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Application for Revisions to the Prevention of Significant Deterioration (PSD)/Permit to Install (PTI) Approvals for Ironville HBI Facility, Toledo, Ohio Permit Number P0123395 Submitted to: City of Toledo Division of Environmental Services 348 S. Erie St. Toledo, OH 43604 Ohio Environmental Protection Agency Division of Air Pollution Control P.O. Box 1049 Columbus, OH 43216-1049 Prepared by: RTP Environmental Associates, Inc. 304-A West Millbrook Rd. Raleigh, NC 27609 Submitted by: IronUnits, LLC July 2019 (Revised September 2019)

Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

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Page 1: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Application for Revisions to the Prevention of Significant Deterioration (PSD)/Permit to Install (PTI) Approvals for

Ironville HBI Facility, Toledo, Ohio Permit Number P0123395

Submitted to:

City of Toledo Division of Environmental Services

348 S. Erie St. Toledo, OH 43604

Ohio Environmental Protection Agency

Division of Air Pollution Control P.O. Box 1049

Columbus, OH 43216-1049

Prepared by:

RTP Environmental Associates, Inc. 304-A West Millbrook Rd.

Raleigh, NC 27609

Submitted by:

IronUnits, LLC

July 2019 (Revised September 2019)

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TABLE OF CONTENTS

1. Introduction and Summary .......................................................... 1-1 1.1 Introduction ..................................................................................................... 1-1 1.2 Project Schedule ............................................................................................ 1-1 1.3 PTI Revision Application ................................................................................. 1-1

2. Project Changes ........................................................................... 2-1 2.1 Project Overview ............................................................................................ 2-1 2.2 Overview of Project Revisions ........................................................................ 2-1 2.3 General Updates to Project Components ....................................................... 2-1 2.4 Material Handling Equipment Changes .......................................................... 2-2 2.5 Updated MIDREX Information Regarding CO Rates ...................................... 2-3

3. Emissions Calculations Changes ............................................... 3-1 3.1 Regulated NSR Pollutants Emissions ............................................................. 3-1 3.2 Changes to Emissions from Emergency Equipment ....................................... 3-1 3.3 Changes to Stack Parameters ........................................................................ 3-1 3.4 Oxide Pellets Sulfur Content Change ............................................................. 3-1 3.5 Fugitive Leaks from Piping Components Updates .......................................... 3-2 3.6 Pressure Relief Vent/Flare Revision ............................................................... 3-2 3.7 Ammonia Emissions from Cooling Water ....................................................... 3-2 3.8 Exempt Natural Gas Combustion Heaters ...................................................... 3-2 3.9 Material Handling Emissions Estimates Changes .......................................... 3-3 3.10 Emissions Information for Core Plant ............................................................. 3-3 3.11 Summary of Project Potential to Emit (Revised) ............................................. 3-3 3.12 Changes to PTI Limits .................................................................................... 3-5

4. Regulatory Applicability Review ................................................. 4-1 4.1 State Regulations ........................................................................................... 4-1

4.1.1 Ohio Revised Code 3745.11 Fees ............................................................. 4-1 4.1.2 OAC 3745-31 Permit to Install New Source of Air Pollution ....................... 4-1

4.2 Federal Regulations ....................................................................................... 4-3 4.2.1 New Source Performance Standards (40 CFR Part 60) ............................. 4-3 4.2.2 National Emissions Standards for Hazardous Air Pollutants (40 CFR Part

63) 4-4

5. Best Available Control Technology ............................................ 5-1 5.1 BACT Applicability .......................................................................................... 5-1 5.2 BACT General Approach ................................................................................ 5-1

5.2.1 Best Available Control Technology Definition ............................................ 5-1 5.2.2 Methodology for the BACT Analysis ........................................................... 5-3

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5.2.3 Basic Purpose and Design of the Project ................................................... 5-3 5.2.4 BACT Baseline ........................................................................................... 5-4 5.2.5 Available Control Strategies ....................................................................... 5-4 5.2.6 BACT Technical Feasibility Criteria ............................................................ 5-5

5.3 HBI Process Overview .................................................................................... 5-5 5.4 Oxide Handling Systems (Enclosed) PM/PM10/PM2.5 BACT Analysis ......... 5-7

5.4.1 PM/PM10/PM2.5 BACT Baseline ............................................................... 5-7 5.4.2 Step 1 – Identify Available PM/PM10/PM2.5 Control Options .................... 5-7 5.4.3 Step 2 – Eliminate Technically Infeasible PM/PM10/PM2.5 Controls ......... 5-8 5.4.4 Step 3 – Rank PM/PM10/PM2.5 Control Options ....................................... 5-8 5.4.5 Step 4 – Evaluate Feasible PM/PM10/PM2.5 Control Options .................. 5-8 5.4.6 Step 5 – Establish PM/PM10/PM2.5 BACT ................................................ 5-9

5.5 Oxide Transfers (open) Operations PM/PM10/PM2.5 BACT Analysis ........... 5-9 5.5.1 PM/PM10/PM2.5 BACT Baseline ............................................................... 5-9 5.5.2 Step 1 – Identify Available PM/PM10/PM2.5 Control Options .................... 5-9 5.5.3 Step 2 – Eliminate Technically Infeasible PM/PM10/PM2.5 Controls ....... 5-10 5.5.4 Step 3 – Rank PM/PM10/PM2.5 Control Options ..................................... 5-10 5.5.5 Step 4 – Evaluate Feasible PM/PM10/PM2.5 Control Options ................ 5-10 5.5.6 Step 5 – Establish PM/PM10/PM2.5 BACT .............................................. 5-10

5.6 Shaft Furnace Bottom Seal Gas Exhaust CO Analysis ................................ 5-10 5.6.1 CO BACT Baseline .................................................................................. 5-11 5.6.2 Step 1 – Identify Available CO Control Options ....................................... 5-11 5.6.3 Step 2 – Eliminate Technically Infeasible CO Control Options ................. 5-11 5.6.4 Step 3 – 5 Bottom Seal Gas Exhaust BACT for CO ................................. 5-11

5.7 Bottom Seal Gas Exhaust GHG Analysis ..................................................... 5-12 5.7.1 GHG BACT Baseline ................................................................................ 5-12 5.7.2 Step 1 – Identify Available GHG Control Options ..................................... 5-12 5.7.3 Step 2 – Eliminate Technically Infeasible GHG Control Options .............. 5-12 5.7.4 Step 3 – 5 Bottom Seal Gas Exhaust BACT for GHG .............................. 5-13

5.8 Hot Briquette Machine Exhaust CO Analysis ............................................... 5-13 5.8.1 CO BACT Baseline .................................................................................. 5-13 5.8.2 Step 1 – Identify Available CO Control Options ....................................... 5-13 5.8.3 Step 2 – Eliminate Technically Infeasible CO Control Options ................. 5-13 5.8.4 Step 3 – 5 Hot Briquette Machine Exhaust BACT for CO ........................ 5-13

5.9 Briquette Cooling System Vapor Removal Vent CO Analysis ...................... 5-14 5.9.1 CO Baseline ............................................................................................. 5-14 5.9.2 Steps 1 - 3 – CO Control Options ............................................................. 5-14 5.9.3 Step 4 - 5 – Establish CO BACT .............................................................. 5-14

5.10 Degasser Exhaust CO and GHG BACT Analyses ........................................ 5-14 5.10.1 Degasser Exhaust CO BACT Analysis ..................................................... 5-15 5.10.2 Degasser Exhaust GHG BACT Analysis .................................................. 5-15

5.11 Pressure Relief Vent/Flare NOx, CO, and GHG BACT Analyses ................. 5-17 5.11.1 NOx, CO, GHG BACT Baselines ............................................................. 5-17 5.11.2 Step 1 – Identify Available NOx, CO, GHG Control Options .................... 5-17 5.11.3 Step 2 – Eliminate Technically Infeasible NOx, CO, GHG Controls ......... 5-17 5.11.4 Step 3 – 5 Flare BACT for NOx, CO, GHG .............................................. 5-17

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5.12 Emergency Engines BACT Analyses ........................................................... 5-18 5.12.1 Emergency Engines PM/PM10/PM2.5 BACT Analysis ............................ 5-18 5.12.2 Emergency Engines NOx BACT Analysis ................................................ 5-20 5.12.3 Emergency Engines CO BACT Analysis .................................................. 5-22 5.12.4 Emergency Engines GHG BACT Analysis ............................................... 5-23

5.13 Equipment Leaks GHG BACT Analysis ........................................................ 5-24 5.13.1 GHG BACT Baseline ................................................................................ 5-25 5.13.2 Step 1 – Identify Available Control Options .............................................. 5-25 5.13.3 Step 2 – Eliminate Technically Infeasible Options.................................... 5-25 5.13.4 Step 3 – Rank Control Options ................................................................ 5-25 5.13.5 Step 4 – Evaluate Feasible Control Options ............................................ 5-25 5.13.6 Step 5 – Establish BACT .......................................................................... 5-26

5.14 HBI Handling Systems (Enclosed) PM/PM10/PM2.5 BACT Analysis ........... 5-26 5.14.1 PM/PM10/PM2.5 BACT Baseline ............................................................. 5-26 5.14.2 Step 1 – Identify Available PM/PM10/PM2.5 Control Options .................. 5-27 5.14.3 Step 2 – Eliminate Technically Infeasible PM/PM10/PM2.5 Controls ....... 5-27 5.14.4 Step 3 – Rank PM/PM10/PM2.5 Control Options ..................................... 5-27 5.14.5 Step 4 – Evaluate Feasible PM/PM10/PM2.5 Control Options ................ 5-28 5.14.6 Step 5 – Establish PM/PM10/PM2.5 BACT .............................................. 5-28

5.15 HBI Transfers (open) Systems PM/PM10/PM2.5 BACT Analysis ................ 5-28 5.15.1 PM/PM10/PM2.5 BACT Baseline ............................................................. 5-28 5.15.2 Step 1 – Identify Available PM/PM10/PM2.5 Control Options .................. 5-28 5.15.3 Step 2 – Eliminate Technically Infeasible PM/PM10/PM2.5 Controls ....... 5-29 5.15.4 Step 3 – Rank PM/PM10/PM2.5 Control Options ..................................... 5-29 5.15.5 Step 4 – Evaluate Feasible PM/PM10/PM2.5 Control Options ................ 5-29 5.15.6 Step 5 – Establish PM/PM10/PM2.5 BACT .............................................. 5-29

5.16 Front End Loaders Movement on Unpaved Surfaces PM/PM10/PM2.5 BACT Analysis ........................................................................................................ 5-30

5.16.1 PM/PM10/PM2.5 BACT Baseline ............................................................. 5-30 5.16.2 Step 1 – Identify Available PM/PM10/PM2.5 Control Options .................. 5-30 5.16.3 Step 2 – Eliminate Technically Infeasible PM/PM10/PM2.5 Controls ....... 5-31 5.16.4 Step 3 – Rank PM/PM10/PM2.5 Control Options ..................................... 5-31 5.16.5 Step 4 – Evaluate Feasible PM/PM10/PM2.5 Control Options ................ 5-31 5.16.6 Step 5 – Establish PM/PM10/PM2.5 BACT .............................................. 5-31

5.17 Trucks Movement on Paved Roads PM/PM10/PM2.5 BACT Analysis ......... 5-31 5.17.1 PM/PM10/PM2.5 BACT Baseline ............................................................. 5-32 5.17.2 Step 1 – Identify Available PM/PM10/PM2.5 Control Options .................. 5-32 5.17.3 Step 2 – Eliminate Technically Infeasible PM/PM10/PM2.5 Controls ....... 5-32 5.17.4 Step 3 – Rank PM/PM10/PM2.5 Control Options ..................................... 5-32 5.17.5 Step 4 – Evaluate Feasible PM/PM10/PM2.5 Control Options ................ 5-33 5.17.6 Step 5 – Establish PM/PM10/PM2.5 BACT .............................................. 5-33

6. Ambient Air Quality Impacts Analysis ........................................ 6-1 6.1 Emissions Rates for Modeling Purposes ........................................................ 6-1 6.2 Summary of Class II Modeled Impacts ........................................................... 6-1

6.2.1 Class II Significant Impacts Analysis .......................................................... 6-1

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6.2.2 Summary of NAAQS Analysis .................................................................... 6-2 6.2.3 Class II PSD Increment Analysis................................................................ 6-2 6.2.4 Visibility Analysis in Class II Areas ............................................................. 6-3

7. Site Air Quality Analysis .............................................................. 7-1

8. Additional Impacts Analyses ....................................................... 8-1 8.1 Effects on Soil................................................................................................. 8-1

8.1.1 Soil Survey ................................................................................................. 8-1 8.1.2 Pollutant Impacts on Soils .......................................................................... 8-2

8.2 Effects on Vegetation ..................................................................................... 8-3 8.2.1 Vegetation Survey ...................................................................................... 8-3 8.2.2 Identification of Pollutants of Concern ........................................................ 8-4 8.2.3 Determination of Effects Concentrations .................................................... 8-5 8.2.4 Results ....................................................................................................... 8-6

8.3 Soil and Vegetation Analysis Conclusion ....................................................... 8-7 8.4 Visibility .......................................................................................................... 8-7 8.5 Growth Impact Analysis .................................................................................. 8-7

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LIST OF TABLES

Table 2-1. Changes to the Material Handling Rates .................................................................... 2-2 Table 3-1. Natural Gas Piping Components ................................................................................ 3-2 Table 3-2. Revised Maximum CO Emission Rates for Core Plant.............................................. 3-3 Table 3-3. Summary of Project PTE (Revised) ........................................................................... 3-4 Table 4-1. PSD Requirements for PTI Revision Application ...................................................... 4-2 Table 4-2. NSPS IIII Requirements for the 311 HP Fire Pump booster engine .......................... 4-3 Table 4-3. NSPS IIII Requirements for the 133 HP Emergency Engine ..................................... 4-3 Table 5-1. Unit-Pollutant Combinations Subject to BACT Review as Part of the Proposed Project

Revisions .............................................................................................................................. 5-1 Table 5-2. Summary of BACT Determinations for the Proposed Project Revisions .................. 5-2 Table 5-3. Summary of PM/PM10/PM2.5 BACT Precedence for Oxide Handling ................... 5-7 Table 5-4. PTE of CH4 from the Project Equipment Components ............................................ 5-25 Table 5-5. Control Costs for Natural Gas LDAR Program ....................................................... 5-26 Table 5-6. Summary of PM/PM10/PM2.5 BACT Precedence for HBI Handling .................... 5-27 Table 5-7. Summary of PM/PM10/PM2.5 BACT Precedence for Unpaved Roads .................. 5-30 Table 5-8. Summary of PM/PM10/PM2.5 BACT Precedence for Paved Roads ...................... 5-32 Table 6-1. Class II Significant Impact Analysis Result ............................................................... 6-2 Table 6-2. NAAQS Analysis Result ............................................................................................ 6-2 Table 6-3. Increment Analysis Result .......................................................................................... 6-3 Table 8-1. Major Soil Types in Study Area ................................................................................. 8-2 Table 8-2. Land Use for Commercially Significant Vegetation in Study Area1,2 ....................... 8-4

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APPENDICES Appendix A PTI Application Forms Appendix B Emissions Calculations Appendix C BACT Cost Table Appendix D Air Dispersion Modeling Report Appendix E Exempt Natural Gas Combustion Equipment Appendix F Updated Process Flow Diagrams

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1. Introduction and Summary

1.1 Introduction IronUnits LLC (“IU”), a subsidiary of Cleveland-Cliffs Inc., obtained a prevention of significant deterioration (PSD) approval and a permit to install (PTI) for a proposed Hot Briquetted Iron (HBI) / Direct Reduced Iron (DRI) manufacturing facility (“HBI Facility”) at the Ironville brownfield site (“Ironville”) in Toledo, Lucas County, Ohio, altogether identified as the “Project.” The Project uses the Midrex Technologies, Inc. MIDREX® natural gas-based direct reduction process to produce 2.48 million tons per year of HBI or DRI from taconite pellets (“oxide”). The Project is located on an approximately 130-acre site adjacent to the southwest corner of Millard Ave and Front Street within the city of Toledo, in Lucas County, Ohio. The Project is a major stationary source under the PSD preconstruction permitting regulations and it was subject to the PSD requirements under Ohio Administrative Code (OAC) 3475-31-11 through 20. Ohio Environmental Protection Agency (“OEPA”) issued a PTI approval P0123395 for the proposed Project on February 9, 2018.

1.2 Project Schedule The construction on the Project commenced in April 2018. Onsite oxide delivery and storage is expected to start in November 2019. IU is currently scheduled to begin operation around April 2020.

1.3 PTI Revision Application Construction for the Project is underway at the Ironville site. Recently, IU received updated information from MIDREX, the HBI/DRI process technology provider, regarding the expected emissions rates from the Core Plant for HBI/DRI production.1 In addition, as the final engineering is being completed and equipment design specifications are finalized, there are updates and additions to the equipment initially proposed under the PTI. This document is IU’s application for a PTI revision approval for the equipment and emissions changes that affect some of the sources permitted under PTI P0123395. This section is the introduction and summary of the application. Section 2 presents a description of the proposed changes. Section 3 presents changes to emissions calculations and proposed limitations. Section 4 presents a regulatory applicability analysis. Sections 5 through 8 address PSD requirements pertaining to this PTI revision application.

1 “Core Plant” refers to the natural gas reformer, HBI/DRI furnace, briquetting process, and other operations that form the heart of the Project.

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2. Project Changes This section presents the proposed revisions to the Project scope and addresses changes and additions to the equipment addressed in the PTI (P0123395).

2.1 Project Overview IU’s basic purpose and fundamental objective for the Project is to construct a DRI/HBI manufacturing facility using natural gas based reducing gas (from reformer process) to produce high carbon content DRI/HBI. The facility will use iron pellets and natural gas as feedstock. The proposed DRI/HBI production process will use the first commercial application in the world of the MIDREX adjustable carbon technology (ACT) to produce varying carbon content in the product (as high as 4.2%). These characteristics are essential in realizing the project objectives of meeting steel industry customer demand in IU’s initiative to produce sustainable steel making raw materials and to make the HBI competitive to commercial grades of pig iron. The DRI process consists of two main components, a natural gas reformer (to produce the reducing agent) and the shaft furnace (where the reaction occurs). The DRI process converts pre-processed iron oxide pellets into highly metallized iron in the form of DRI, which is then briquetted to form HBI. MIDREX’s novel ACT system allows for the addition of more natural gas at higher temperatures in the transition zone of the furnace in order to impart higher carbon to the DRI/HBI product. Detailed description of the process equipment and associated operations was provided in the application submitted on December 5, 2017 for the PTI (P0123395) issuance. Updated process flow diagrams are included as Appendix F.

2.2 Overview of Project Revisions After completing the detailed engineering process in coordination with the engineering and equipment providers, IU is proposing the following three categories of revisions for the Project that require PTI revision approval from OEPA:

(a) General updates to Project components (b) Material handling equipment changes (c) Updated information regarding CO emission rate estimates from MIDREX

This application addresses only the equipment and emissions rates changes or equipment additions for the Project (“Project revisions”) as outlined in the following subsections. The equipment/emissions estimate that remain unchanged from PTI P0123395 are not addressed in this PTI revision application.

2.3 General Updates to Project Components Based on the final engineering and equipment design specifications, IU identified the following set of general changes. The updated emissions calculations reflecting these changes are provided in Appendix B.

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(a) Minor changes to the stack parameters for several emissions units. These include changes to the stack heights, stack diameters, exhaust gas temperature, and exhaust flowrates. Where necessary, the particulate matter emissions rates are adjusted to reflect the revised stack parameters specifications.

(b) MIDREX revised the SO2 emission rate from the Project based on final oxide pellets sulfur content specification. The overall SO2 emissions increase for the Project remains below the PSD significant emission rate of 40 tons per year.

(c) The fire water pump (for emergency use) P006 engine capacity is increased from 250 hp to 311 hp.

(d) A 133 hp emergency diesel-fired engine generator is added as P-10. This unit is needed for the administrative building at the site.

(e) Updated the fugitive leaks components based on the updated information from MIDREX and site engineering.

(f) For the pressure relief vent/flare, we corrected the gas flowrate to 99,520 scfm (prior application erroneously used 99,250 scfm).

(g) MIDREX provided estimated ammonia (NH3) emissions from the cooling water circuit for the process. Based on the engineering evaluation, NH3 may be released from the process water Degasser and/or the Cooling Tower exhaust.

(h) Several small natural gas-fired space heaters are to be installed in various buildings at the site. Each of these units will have heat input capacity no greater than one (1) MMBtu per hour. Detailed list of these units is provided in Appendix E.

2.4 Material Handling Equipment Changes The final engineering designs for various material handling operations resulted in changes to the maximum hourly throughput rates for several pieces of equipment (transfer and handling operations) for oxide pellets and HBI. In addition, based on the updated oxide pellets fines content information, the annual throughput rate for oxide fines is also revised. These changes to the maximum hourly and annual throughput rates are shown in Table 2-1 below and affect operations under P901, P902, and F002 emissions units in the PTI.

Table 2-1. Changes to the Material Handling Rates Operation Permit Emission

Unit Prior Throughput

Rate Updated Throughput

Rate Oxide transfer from Midwest TR-1, TR-2, TR-3 (and associated operations at Midwest Terminal)

P901 3,310 tons/hour 3,970 tons/hour

Oxide reclaim and transfer from stockpile TR-4, TR-5, TR-6, and TR-7

P901, F002 1,220 tons/hour 1,460 tons/hour

Oxide transfers from day bins TR-10, SR-1, TR-13a P901 470 tons/hour 560 tons/hour Oxide lumps operation TR-8 F002 1.2 tons/hour 24.3 tons/hour Oxide fines operations TR-11 F002 24 tons/hour and

71,893 tons/year 46 tons/hour and 215,680 tons/year

Oxide fines operations FEL-2, TR-12, HR-2 F002, F001 28 tons/hour and 71,893 tons/year

28 tons/hour and 215,680 tons/year

HBI transfers to stockpile TR-17, TR-18, TR-19, TR-20 P902 320 tons/hour 510 tons/hour HBI reclaim (using bucket elevator) and other operations TR-23 and TR-24

P902 566 tons/hour 800 tons/hour

REMET operations F002 14 tons/hour 17 tons/hour Truck loadout operations TR-25 P902 170 tons/hour 500 tons/hour (6,000

tons/day) Rail loadout operations TR-26 P902 566 tons/hour 1,000 tons/hour (12,000

tons/day)

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In addition, the initial project design assumed use of front end loaders (FELs) to reclaim HBI from the stockpile. However, the final project design will use a bucket wheel reclaim system for HBI reclaim from the stockpile. The bucket wheel reclaim system will include two transfer points TR-21a and TR-21b. This system will operate at a maximum transfer rate of 800 tons/hour (24-hour average). This change will affect the HBI handling operations under P902 and F002. IU is retaining the ability reclaim using FELs as backup with maximum annual rate no greater than 500,000 tons/year. In addition to the items noted above, IU is proposing the following additional changes to the previously permitted material handling operations.

(a) Some of the HBI conveyor transfer points (e.g. TR-18, TR-23) that were previously proposed with venturi scrubbers particulate matter controls will now be equipped with baghouses for particulate matter controls. The design grain loading for the baghouses will be the same as the original venturi scrubber design. This reduces amount of liquid waste to be handled at the site.

(b) Under P901, a new emission point is added for transfer of oxide to furnace feed conveyor TR-28a. This oxide transfer operation will be controlled by a baghouse.

(c) Previously IU planned to use the coating storage and mixing baghouse to also control emissions from the fines conveyor transfer point. Under the revised design, a new baghouse will now control fines transfer point TR-13b and a smaller baghouse will control emissions from the coating storage. This is not a new transfer point, but due to addition of a new baghouse, the equipment description for P901 will change.

(d) A new furnace feed recovery operation is required for recovery of oxide from the furnace charging operation in case of production upset. The feed recovery system will include transfer to stockpile TR-29, stockpile wind erosion WE-6, reclaim using FEL (FEL-5) and transfer to hopper TR-30. These operations are to be included under F002.

(e) The HBI stockpile will require a product oversize transfer operation. The proposal is to use an enclosed structure for this operation. Thus, the emissions will only occur from reclaim by front end loader FEL-6 and transfer to hopper TR-31. These operations are also to be included under F002.

(f) A new activity was identified as transport of wastewater sludge by trucks. This activity is designated as HR-5 and added as part of the oxide material handling and transport operations. This operation is to be included under F001.

In the initial PTI application, an oxide conveyor transfer tower controlled by a baghouse MTR-5 was included at the Midwest terminal as part of “secondary emissions” from the project. This transfer point and baghouse was included in the air quality modeling for the project. IU has now decided to include MTR-5 as part of its revised PTI and is requesting that this emission point be included under P901.

2.5 Updated MIDREX Information Regarding CO Rates The MIDREX technology provides a unique and innovative DRI manufacturing process that uses reformed natural gas to produce direct reduced iron from oxide pellets. Numerous MIDREX DRI facilities are in operation throughout the world, including one domestic facility which uses this technology, however, very limited actual CO emission testing data was available until recently. Additionally, the IU DRI/HBI production process installation in Toledo will be the first

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commercial application in the world to use the new MIDREX ACT system which produces varying carbon content of the DRI product. IU’s utilization of the MIDREX ACT is essential for meeting the project’s objectives of satisfying steel industry customer demand to produce sustainable steel making raw materials and to make the HBI carbon content competitive to commercial grades of pig iron. In IU’s original PTI application submittal, CO rates for various components in the DRI production process (“Core Plant”) were developed by MIDREX based on engineering estimates and limited testing information available from other existing facilities. Since the time of original PTI application submittal, MIDREX has collected additional CO emission testing data for some of the Core Plant emission points from existing MIDREX facilities and has updated its proprietary emission estimating model to more accurately characterize CO emission rates for the Core Plant while producing HBI using MIDREX ACT system. MIDREX recently notified IU of its capabilities to refine previous CO emissions estimates. IU then requested MIDREX to re-estimate CO emission rates for the IU facility by taking into account the updated underlying information and IU-specific project design considerations such as IU production rates and IU’s unique ability to vary carbon content in the DRI/HBI product via the ACT system based on the customer specifications. MIDREX provided updated CO emission rates along with explanation for the adjustment for the following Core Plant components:

• Bottom Seal Gas Exhaust: Midrex updated its IU-specific emission model to account for: o Stack test data: New CO stack test data was collected from existing, operating

MIDREX facilities; o Solid state carbon reactions: CO is generated from solid state carbon

reactions (FeO + C -> Fe + CO) in the Product Discharge Chamber. Higher carbon DRI/HBI production is the primary contributor to higher estimated CO emissions due to the increased availability of carbon for this reaction to occur.

o DRI Fines Variability: The Bottom Seal Gas dust collection system uses dilution air to safely transport metalized fines to the wet scrubber. These fines cool rapidly but can partially combust when mixed with air, especially when the fines concentration is high. Recent test data under high fines conditions has shown an increase in the CO levels emitted from the dust collection systems.

o Iron Oxide Feed Variability: Variations in raw material fed to the DRI reactor can influence the amount of CO produced in the downstream systems. Reactivity of the ore, porosity, tendency to carburize, and pellet strength can all affect how much CO is generated.

o Depressurization: The sponge iron (DRI) contains CO in its pore space and when the DRI enters the Product Discharge Chamber, a portion of the CO in its pore space is released due to pressure in the Product Discharge Chamber being less than the pressure in the upstream Reduction Furnace.

o Re-oxidation Reactions: When discharged from the shaft furnace, the DRI temperature is >650 °C which will continue to generate CO when the product and associated fines re-oxidize (Fe + CO2 -> FeO + CO and 2C + O2 -> 2CO) downstream of the bottom seal gas leg.

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• Hot Briquette Machine Exhaust: Midrex updated its IU-specific emission model to account for:

o Test data: New CO test data was collected from existing, operating MIDREX facilities;

o Solid state carbon reactions: CO can be generated from ongoing solid state carbon reactions (FeO + C -> Fe + CO) due to high product temperatures at the briquetting operation. Higher carbon DRI/HBI production is the primary contributor to higher estimated CO emissions due to the increased availability of carbon for this reaction to occur.

o DRI Fines Variability – The Hot Briquette dust collection system uses dilution air to safely transport metalized fines to the wet scrubber. These fines cool rapidly but can partially combust when mixed with air, especially when the fines concentration is high. Recent test data under high fines conditions has shown an increase in the CO levels emitted from the dust collection systems.

o Re-oxidation Reactions: While the reactivity of the DRI is substantially reduced once the material is compressed into briquettes, any small material such as fines and chips downstream of the briquetters can re-oxidize and form CO (Fe + CO2 -> FeO + CO and 2C + O2-> 2CO).

o Compression of sponge iron: The briquetting machine compresses sponge iron (DRI) into dense HBI. The sponge iron still contains some CO in its pore space and compression in the briquetter releases pore space CO.

• Briquette Cooling System Vapor Removal Vent: Midrex updated its IU-specific emission

model to account for: o Test data: New CO test data was collected from existing, operating MIDREX

facilities; o Re-oxidation Reactions: While the reactivity of the DRI is substantially reduced

once the material is compressed into briquettes, any small material such as fines and chips downstream of the briquetters can re-oxidize and form CO (Fe + CO2 -> FeO + CO and 2C + O2-> 2CO).

o Water Reactions: Water sprays used for cooling the HBI can react with the carbon in the product to form CO (H2O + C -> CO + H2)

o Solid state carbon reactions: CO can be generated from ongoing solid state carbon reactions (FeO + C -> Fe + CO) due to high product temperatures at the entrance of the Briquette Cooling Conveyor. Higher carbon HBI production is the primary contributor to higher estimated CO emissions due to the increased availability of carbon for this reaction to occur.

• Degasser Exhaust: The Top Gas Scrubber utilizes water to remove particulate from the

top gas. The scrubber water will contain dissolved CO and when the scrubber water is exposed to lower pressure in the degasser system, CO can be released. Midrex updated its IU-specific emission model to account for the maximum CO solubility in water (0.01 grams CO/kg of water at 1 atm and 80 degrees Celsius).

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3. Emissions Calculations Changes The proposed Project revisions due to final engineering and updated equipment specifications since the original permit application result in changes to estimated emissions of regulated NSR pollutants from some of the operations. These changes in emissions are described in this section. IU followed the same methodologies as the original PTI application for estimating revised emissions from the Project. Detailed emissions calculations are included in Appendix B.

3.1 Regulated NSR Pollutants Emissions The regulated NSR pollutants included here are particulate matter (PM), particulate matter equal to or less than an aerodynamic diameter of nominally 10 µm (PM10) and 2.5 µm (PM2.5), oxides of nitrogen (NOx), carbon monoxide (CO), volatile organic compounds (VOC), sulfur dioxide (SO2), lead (Pb), and greenhouse gases (GHGs) as carbon dioxide equivalent (CO2e). CO2e is calculated in accordance with 40 CFR §52.21(b)(49)(ii) using the mass emission rates of six GHGs2 defined in 40 CFR §52.21(b)(49)(i) and corresponding global warming potential (GWP) published in 40 CFR 98, Subpart A, Table A-1. For this application, Table A-1 GWPs from the July 1, 2015 version of the 40 CFR Part 98 are used. The OEPA application forms (Appendix A) require uncontrolled potential to emit (PTE) information. Where this information was not readily available, we conservatively back calculated uncontrolled PTE using the controlled emission rate and the control efficiency for the control device.

3.2 Changes to Emissions from Emergency Equipment As previously noted, the rated output for the engine in the emergency firewater pump P009 is increased to 311 hp to accommodate recent revisions to the specifications after the initial permit application. In addition, the updated Project design includes a new emergency generator for the Administration building. Emissions from the two emergency engines affected by this Project revision are estimated using the equipment specifications and the applicable new source performance standard (NSPS) limitations (presented in section 4.2.1.

3.3 Changes to Stack Parameters Minor changes to stack parameters based on design changes since the last permit application resulted in changes to particulate matter (PM/PM10/PM2.5) model inputs for some of the equipment. IU updated the model input to reflect the revised stack parameters.

3.4 Oxide Pellets Sulfur Content Change To accommodate changes in the final pellet sulfur content specification for the oxide pellets, MIDREX revised the SO2 emissions rates for two emission points in the Core Plant.

2 The aggregate group of six greenhouse gases are: carbon dioxide, nitrous oxide, methane, hydrofluorocarbons, perfluorocarbons, and sulfur hexafluoride. (40 CFR § 52.21(b)(49)(i))

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(a) Reformer exhaust B001 (b) Hot briquette exhaust P002

3.5 Fugitive Leaks from Piping Components Updates Updated information regarding the estimated number of natural gas piping components such as, gas service valves, pressure relief valves, and connectors was obtained from the final engineering documentation. Table 3-1 lists the final component counts for natural gas piping at the plant (IU added 10% margin as contingency to account for unforeseen changes when installing the final natural gas piping).

Table 3-1. Natural Gas Piping Components Piping Component Number Valves – gas service 418 Pressure relief valves 54 Connectors 1,982

IU followed the previously used methodology to estimate fugitive VOC and GHG emissions from the natural gas piping component leaks. We conservatively assumed that all of the components listed above will be threaded or otherwise could result in natural gas leaks.

3.6 Pressure Relief Vent/Flare Revision Emissions from the flare during process startup/shutdown events are revised based on new information to correct the gas flowrate to the flare and using the same methodology as the original PTI application. This resulted in small increases in emissions of some of the regulated NSR pollutants as noted in Appendix B.

3.7 Ammonia Emissions from Cooling Water Based on updated emission information from MIDREX, the estimated NH3 emission for the Degasser exhast is approximately four pounds per hour. Based on the MIDREX information we have conservatively estimated NH3 emisisons from the Cooling Tower exhaust to be 2.25 pounds per hour.

3.8 Exempt Natural Gas Combustion Heaters Updated information for the Project includes installation of several small natural gas fired heaters that meet the criteria for ‘de minimis’ air contaminant source under OAC 3745-15-05. A list of these small exempt heaters is provided in Appendix E of this application. De minimis sources are exempt from Ohio air pollution rules in accordance with Ohio Revised Code 3704.011 and excluded from further consideration in the revised PTI for the Project.

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3.9 Material Handling Emissions Estimates Changes The PM/PM10/PM2.5 emissions estimates are revised to reflect the updated information presented in subsection 2.4. The new baghouses proposed under the revised design will retain the outlet particulate matter grain loading specification of 0.0025 grain per dry standard cubic feet, same as the ones already in the PTI. Updated short term and annual throughput assumptions are used to update the emissions estimates from various material handling equipment. Daily and annual fugitive emissions from trucks haul roads are revised to reflect the new information on daily and annual throughput rates. Specifically, the HBI loadout by trucks is based on the proposed maximum truck loadout rate of 6,000 tons per day. In addition, for train loadout, the daily emissions rates are based on 12,000 tons per day throughput. New information also updates the estimated emissions from the transfer of wastewater sludge using trucks on paved roads using the same methodology as the original PTI application. The truck travel distance is estimated to be 0.73 miles round trip.

3.10 Emissions Information for Core Plant The DRI technology supplier, MIDREX, updated their Core Plant equipment CO emission estimates based on updated emission test data obtained from other MIDREX facilities and associated refinements made to the emissions modelling tool to simulate emission rates at various process rates (DRI carbon concentrations, metallization rates, process throughput rates, etc.). Table 3-2 presents the revised CO emissions rates for the Core Plant emission points.

Table 3-2. Revised Maximum CO Emission Rates for Core Plant Emission Point CO Emissions (lb/hour) P001 Charge Hopper Scrubber Exhaust (No Change) 2.8 P001 Bottom Seal Gas Scrubber Exhaust 986.0 B001 Reformer Heater Exhaust (No change) 52.35 P002 Hot Briquette Scrubber Exhaust 912.0 P003 Briquette Cooling System Scrubber Exhaust 594.08 P004 Process Water Degasser Exhaust 110.6 P008 Flare (Due to flow correction) 554.06

Further discussion of emissions points, where CO rates are revised, is presented under BACT in Section 5 of this application.

3.11 Summary of Project Potential to Emit (Revised) Table 3-3 summarizes the revised PTE of regulated NSR pollutants for the HBI facility. Detailed emissions calculations are provided in Appendix B. SO2 and VOC PTE remains below the PSD significant emission rates. Overall NOx emissions rate increased due to addition of a new emergency generator and the fire water pump engine output capacity increase. However, there are no increases in NOx emissions from the other permitted emissions units. For the pollutant/equipment combinations highlighted in Table 3-3, IU included updated BACT analyses in section 5 of this application.

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Table 3-3. Summary of Project PTE (Revised)

Emissions (tons/year) Emission Unit(s)/Groups PM PM10 PM2.5 NOx SO2 CO VOC CO2 CO2e Oxide Storage and Handling 9.06 6.19 4.55 Furnace Charge Hopper Exhaust 0.44 0.44 0.44 8.85 1.05 12.36 5,891 5,891 Bottom Seal Gas Exhaust 11.21 11.44 11.44 1.88 1.05 4,318.80 3,666 3,666 Reformer Exhaust 35.30 81.96 81.96 436.89 22.12 229.29 7.97 1,553,868 1,554,047 Hot Briquette Exhaust 17.39 17.96 17.96 17.25 0.92 3,994.62 54,071 54,071 Briquette Cooling System Vent 14.47 14.47 14.47 2,602.05 Degasser Exhaust 482.05 18,054 18,054 Flare 0.17 0.66 0.66 6.05 0.05 27.57 4.61 10,402 10,413 HBI Storage and Handling 7.80 2.64 1.83 Cooling Tower 0.30 0.09 0.06 0.12 Emergency Fire Water Booster 0.03 0.03 0.03 0.51 0.00 0.45 0.20 98 99 Emergency Generator 0.22 0.25 0.25 7.05 0.01 3.86 0.43 681 683 Admin Building Generator 0.02 0.02 0.02 0.22 0.00 0.27 0.02 38.81 38.95 Fugitive Emissions from Components 3.06 2,757 Total 96.41 136.16 133.68 478.70 25.20 11,671.32 16.40 1,646,771 1,649,721 PSD Significant Emissions Rate 25 15 10 40 40 100 40 -NA- 75,000 Whether Significant? Yes Yes Yes Yes No Yes No Yes Highlighted cells show estimated emissions that are different from the initial PTI permit or are new as part of this revision.

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3.12 Changes to PTI Limits IU understands that the emissions limits in the PTI for the affected sources will be revised based on the updated final information submitted through the Air Services portal. However, we specifically request that the following operating limits in the PTI be removed or revised.

(a) For P902 under 13.b.2.e, the maximum HBI truck loading rate is limited to 743,724 tons per 12-month period. We request that the HBI truck loading rate of 743,724 be deleted and replaced with a new limit of 2,190,000 tons based upon a rolling, 12-month summation of the loading rates. .

(b) For P902 under 13.b.2.f, the maximum HBI train loading rate is limited to 6,792 tons per day. Similar to truck loading above, the 6,792 tons per day limit is to be deleted and replaced with a daily rate of 12,000 tons per day.

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4. Regulatory Applicability Review A review of the potentially applicable federal and Ohio regulations has been conducted for this PTI revision request. The following subsections summarize the applicability of these regulations to the proposed Project updates.

4.1 State Regulations This analysis is based on the version of the Ohio Administrative Code (“OAC”) available at the time this application was prepared.

4.1.1 Ohio Revised Code 3745.11 Fees OAC 3745.11(F) establishes fees for issuance of a permit to install approval for various types of sources including fuel burning equipment, various industrial categories etc. OEPA also provides a fee schedule on its website based on type of equipment to be permitted.3 An upfront application fee is not required and the permitting agency bills the applicants for permit fee prior to PTI issuance.

4.1.2 OAC 3745-31 Permit to Install New Source of Air Pollution In accordance with OAC 3745-31, PTI (P0123395) was issued for the Project by OEPA on February 9, 2018. This application addresses revisions to the PTI issued for the Project to reflect the design and equipment updates outlined here.

4.1.2.1 OAC 3745-31-05(A)(3)(a) Employ BAT OAC 3745-31-05(A)(3) requires BAT for an individual air contaminant source installed after August 3, 2006 that has potential to emit after control of 10 tons per year or more. BACT evaluations satisfy BAT evaluations. The updated Project, increases in SO2 and VOC emissions are below the PSD significant emissions rates. Therefore, emissions of these pollutants from the units under the Project are not subject to PSD BACT requirements and require a separate BAT evaluation. PTE of both VOC and SO2 are below 10 tons per year for all air contaminant sources proposed under the Project, except revised SO2 emissions from the reformer, which are above 10 tons per year (from 18.70 tons per year to 22.12 tons per year. Therefore, only the reformer SO2 emissions are subject to the requirement to employ BAT. The reformer burner will use gaseous fuel (furnace top gas and natural gas), which is a low-sulfur bearing fuel that minimizes the formation of SO2 emissions. Reformer SO2 revised PTE is 22.12 tons per year which is well below the PSD significant emission rate. Add-on SO2 control devices cannot cost effectively reduce SO2 emissions further. Therefore, use of naturally low-sulfur gaseous fuel, comprised of furnace top gas and natural gas, in the reformer is determined as BAT. PTE of NH3 for the Degasser exhaust exceeds 10 tons per year. Therefore, NH3 emissions from this source are subject to the requirement to employ BAT. We are not aware of any similar sources in Ohio that control ammonia emissions and a review of the U.S. EPA’s RBLC database 3 http://www.epa.state.oh.us/portals/47/facts/feeschedule.pdf (last accessed on July 7, 2019).

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did not identify any add-on control technologies for ammonia emissions from similar sources. For some of the petroleum refinery waste streams, catalytic treatment systems can be used for reducing NH3 concentrations. However, such applications involve very low volume streams and relatively high NH3 concentration. These conditions are not present for the Degasser exhaust. Therefore, no add-on controls are technically feasible or qualify as BAT for Degasser. Based on the MIDREX specifications, optimum source design is presumed to be BAT for the Degasser exhaust.

4.1.2.2 OAC 3745-31-11 through 20 Attainment Provisions OAC 3745-31-11 through 20 contain provisions applicable to new major stationary sources or NSR projects that are major modifications for regulated NSR pollutants for which area is attainment. The HBI Facility was permitted as a major stationary source subject to PSD review. This PTI revision application addresses PSD requirements as noted in Table 4-1.

Table 4-1. PSD Requirements for PTI Revision Application

Citation Requirements Application Section Pollutant & Units OAC 3745-31-11 Allowable increments Appendix D Entire Project OAC 3745-31-12 Data submission

authority and minimum data submission requirements

Entire application NA

OAC 3745-31-13 Air pollutants covered 4 NA OAC 3745-31-14 Preapplication

monitoring requirements Appendix D NA

OAC 3745-31-15 Control technology review

5 • PM/PM10/PM2.5 for oxide and HBI material handling operations

• CO and GHGs for some of the Core Plant equipment

• NOx, CO, and GHG BACT for flare

• PM/PM10/PM2.5, NOx, CO, GHGs for Admin Emergency Generator and Emergency Fire Pump

• GHG for fugitive component leaks

OAC 3745-31-16 Source impact analysis 6, Appendix D Entire Project OAC 3745-31-17 Additional impact

analysis 7 Entire Project

OAC 3745-31-18 Air quality models 6, Appendix D Entire Project OAC 3745-31-19 Notification to U.S. EPA

and Federal Land Manager

OEPA obligation; FLM notification provided in prior submittal

NA

OAC 3745-31-20 Innovative control technology

NA NA

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There are no changes to other State regulatory requirements documented in the original PTI application and the PTI for the Project.

4.2 Federal Regulations 4.2.1 New Source Performance Standards (40 CFR Part 60) Applicability of the NSPS requirements for the proposed emergency units is presented below.

4.2.1.1 General Provisions, 40 CFR Part 60, Subpart A IU will comply with the applicable requirements under general provisions of 40 CFR Part 60 Subpart A. These will include notifications, compliance testing, monitoring, recordkeeping and reporting provisions of the rule.

4.2.1.2 Standards of Performance for Stationary Compression Ignition Internal Combustion Engine, 40 CFR Part 60, Subpart IIII

NSPS 40 CFR Part 60, Subpart IIII applies to stationary compression ignition RICE, including fire-pumps that commence construction after 2009.

(1) The proposed fire-pump booster engine will be subject to the requirements of this rule as noted below: (a) Comply with the emission limitations in Table 4-2 below. (40 CFR §§60.4202(d) and

60.4205(c), Table 4)

Table 4-2. NSPS IIII Requirements for the 311 HP Fire Pump booster engine Pollutant Emission Standard (g/HP-hr)

NMHC+NOx 3.0 CO 2.6 PM 0.15

IU plans to purchase a manufacturer certified fire-pump RICE that will be in compliance with the above limitations.

(b) Use ultra-low sulfur diesel fuel per the requirements of 40 CFR §80.510(b). (40 CFR

§60.4207(b))

(2) The proposed emergency engine generator will be subject to the requirements of this rule as noted below:

(a) Comply with the emission limitations in Table 4-3 below from 40 CFR §89.112. (40

CFR §§60.4202(a)(2) and 60.4205(b)) Table 4-3. NSPS IIII Requirements for the 133 HP Emergency Engine

Pollutant Emission Standard (g/kW-hr) NMHC+NOx 4.0

CO 5.0 PM 0.3

40 CFR §89.112(a) Tier II standards for units >560 kW

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IU plans to purchase a manufacturer certified emergency RICE generator that will be in compliance with the above limitations.

(b) Use ultra-low sulfur diesel fuel per the requirements of 40 CFR §80.510(b). (40 CFR

§60.4207(b))

4.2.2 National Emissions Standards for Hazardous Air Pollutants (40 CFR Part 63)

Applicability of the NESHAP requirements for the proposed units is presented below.

4.2.2.1 National Emission Standards for Hazardous Air Pollutants: Stationary Reciprocating Internal Combustion Engines, 40 CFR Part 63, Subpart ZZZZ

NESHAP 40 CFR 63 Subpart ZZZZ applies to RICE located at area and major sources of HAP emissions. The Project, an area source, will involve construction of emergency RICE. Pursuant to 40 CFR § 63.6590(c)(1) new stationary RICE located at an area source that are subject to 40 CFR Part 60 IIII are exempt from 40 CFR Part 63 Subpart A and Subpart ZZZZ.

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5. Best Available Control Technology

5.1 BACT Applicability This section presents the BACT reviews for the proposed Project revisions. The BACT analysis addresses pollutant/emission unit combinations identified in Table 3-3. In the case of the proposed Project revision, BACT is applicable for PM, PM10, PM2.5, NOx, CO, and GHGs to all of the newly added emissions units and all of the units where PTE increased from the prior PTI application. Table 5-1 lists each pollutant/emission unit combination subject to BACT review as part of this PTI revision application for the proposed Project revisions. Table 5-2 lists BACT analyses results for the pollutant/emission unit combinations for the proposed Project revisions.

Table 5-1. Unit-Pollutant Combinations Subject to BACT Review as Part of the Proposed Project Revisions

Unit Description PM/ PM10/ PM2.5 NOx CO GHGs

Oxide Storage and Handling X Bottom Seal Gas Scrubber X X Hot Briquette Exhaust X Briquette Cooling System Vent X Degasser Exhaust X X Flare X X X HBI Storage and Handling X Emergency Fire Water Booster X X X X Admin Emergency Generator X X X X Fugitive Emissions from Leaks X

5.2 BACT General Approach This section presents an outline of the BACT approach for the proposed Project revisions for regulated NSR pollutants subject to PSD review.

5.2.1 Best Available Control Technology Definition The definition of BACT at OAC 3745-31-01(S) is as follows: An emissions limitation (including a visible emission standard) based on the maximum degree of reduction for each regulated NSR pollutant which would be emitted from any proposed major stationary source or major modification which the director, on a case-by-case basis, taking into account energy, environmental and economic impacts and other costs, determines is achievable for such major stationary source or major modification through application of production processes or available methods, systems and techniques, including fuel cleaning or treatment or innovative fuel combustion techniques for control of such pollutant. In no event shall application

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of BACT result in emissions of any pollutant that would exceed the emissions allowed by any applicable standard under 40 CFR Parts 60, 61, and 63. If the director determines that technological or economic limitations on the application of measurement methodology to a particular emissions unit would make the imposition of an emission standard infeasible, a design, equipment, work practice, operational standard, or combination thereof, may be approved by the director instead to satisfy the requirement for the application of BACT. Such standard shall, to the degree possible, set forth the emission reduction achievable by implementation of such design, equipment, work practice or operation and shall provide for compliance by means which achieve equivalent results. This definition of BACT is generally consistent with that in the federal Clean Air Act as amended in 1977.4 The Clean Air Act Amendments of 1990 added the phrase “clean fuels” to the list of candidate methods, systems, and techniques.5 Table 5-2. Summary of BACT Determinations for the Proposed Project Revisions EU ID Unit Description Pollutant Proposed BACT P-6 Flare (During Process Upset and

Startup/Shutdown) NOx, CO, GHGs Flaring minimization plant

design to meet 40 Part 60.18 Flare Pilot NOx, CO, GHGs Use of natural gas and follow

good combustion practices P-1 Bottom Seal Gas Exhaust CO, GHGs Optimum equipment design

and use of N2 seal P-3 Hot Briquette Exhaust CO Optimum equipment design P-4 Briquette Cooling System Vapor

Removal Vent CO Optimum equipment design

P-5 Degasser Exhaust CO, GHGs Optimum equipment design P-8 Emergency Diesel Fire Pump Booster

Engine PM/PM10/PM2.5, NOx, CO

Follow requirements of NSPS Subpart IIII

P-9 Admin Emergency Diesel Generator Engine

PM/PM10/PM2.5, NOx, CO

Follow requirements of NSPS Subpart IIII

P-8, P-9 Emergency Engines GHGs Fuel specific emission factor FugGHG Fugitive Components Leaks GHGs Follow good industrial design Various Oxide Material Handling and Storage

Systems PM/PM10/PM2.5 Baghouses for emission points

with outlet grain loading of 0.0025 gr/dscf. Dust suppression for fugitive operations.

Various HBI Material Handling and Storage Systems

PM/PM10/PM2.5 Scrubbers and baghouses for emission points with outlet grain loading of 0.0025 gr/dscf. Dust suppression for fugitive operations.

4 P.L. 95-95, § 127(a). 5 P.L. 101-549, § 403(d). See, also, current 42 U.S.C. § 7479(3).

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5.2.2 Methodology for the BACT Analysis OEPA’s air quality regulations do not prescribe a procedure for conducting a case-by-case BACT analysis but, by convention, BACT determinations are typically made following the top-down approach. Accordingly, the BACT analyses presented in this application utilize the top-down approach. Under the “top-down” approach, progressively less stringent control technologies are analyzed until a level of control considered BACT is determined, based on the most effective control option that is determined to result in acceptable environmental, energy, and economic impacts. More specifically, the top-down BACT analysis methodology consists of five steps as follows:

1. Identify all “available” control options that might be utilized to reduce emissions of the subject pollutant for the type of unit subject to BACT.

2. Eliminate those available options that are technically infeasible to apply to the specific unit under consideration.

3. Rank the remaining feasible control options by control effectiveness.

4. Evaluate economic, energy and/or environmental impacts of each control option as applied to the subject units, rejecting those options for which the adverse impacts are inappropriate.

5. Based on the most effective control option not rejected in Step 4, select an emission limit or work practice standard as BACT, reflecting the level of control continuously achievable with the selected control option.

5.2.3 Basic Purpose and Design of the Project To determine whether a particular technology or technique is “available” for consideration in the BACT analysis, or would fundamentally redefine the proposed source, and must therefore be omitted from consideration in the BACT analysis “a permitting authority should look first at the administrative record to see how the applicant defined its goal, objectives, purpose or basic design.”6 The permitting authority must take a “hard look” and determine “which design elements are inherent to [the] purpose [of the facility], articulated for reasons independent of air quality permitting, and which design elements may be changed to achieve pollutant emission reductions.”7 IU’s basic purpose, design, and fundamental objective for the Project is to construct a HBI manufacturing facility using natural gas based reducing gas (from reformer process) on the proposed 130 acre site in Lucas County, Ohio. This facility will be designed to produce up to 2.48 million tons of HBI with carbon levels as high as 4.2% using ACT system to meet customer specifications for input to the steel manufacturing operations. The facility will use iron pellets and natural gas as feedstock. The project design requires use of a reformer unit to generate reducing gas by reforming natural gas that will be used in the DRI reactor for producing DRI and HBI. These characteristics are essential in realizing the project objectives for IU’s to produce 6 PSD and Title V Permitting Guidance for Greenhouse Gases, EPA-457/B-11-001, March 2011, at p. 26. 7 In re Prairie State, 13 E.A.D. at 23, 26-27 (EAB 2006).

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sustainable steel making raw materials to meet steel industry customer demands and to make the HBI carbon content competitive to commercial grades of pig iron.

5.2.4 BACT Baseline As used in the BACT analyses presented herein, the term “BACT baseline” refers to the following requirement in the definition of BACT: In no event shall application of BACT result in emissions of any pollutant that would exceed the emissions allowed by any applicable standard under 40 CFR Parts 60, 61, and 63. Thus, any applicable OEPA, State or federal limit on emissions of a BACT-subject regulated NSR pollutant from a given unit serves as a baseline for purposes of the BACT evaluations. As an example, OAC 3745-17-10 (Restrictions on particulate emissions from fuel burning equipment) limits PM emissions to be no greater than 0.020 pound per million Btu of actual heat input.8 This limit serves as the PM BACT baseline for the proposed reformer.

5.2.5 Available Control Strategies In the first step of the BACT analysis, all potentially “available” control strategies are identified for further consideration. In the context of the first step of a top-down BACT analysis, U.S. EPA’s guidance describes “available” control strategies as: [T]hose air pollution control technologies or techniques with a practical potential for application to the emissions unit and the regulated pollutant under evaluation.9[emphasis added] In the BACT analyses herein, the term “available” is used, consistent with the U.S. EPA guidance, to refer to any control strategy that is potentially applicable to the source type in question (i.e., a technology or control option that has a practical potential for application to the source category in general). These may include fuel cleaning or treatment, inherently lower polluting processes, and end of pipe control devices. All identified control strategies that are not inconsistent with the fundamental purpose and basic design of the proposed facility are listed in this step. As discussed in subsection 5.2.6 below, the second step of the BACT analysis addresses site-specific or design-specific criteria that would prevent an otherwise available technology from being applied in the particular case of the proposed project. This “technical feasibility” question is separate and distinct from the criteria used to determine whether a control option is considered to be “available” for purposes of determining BACT.

8 For the purposes of BACT analyses, we did not consider process weight rate rule limitations in OAC 3745-17-11 as baseline as the process weight rate limitations are relatively larger than the PTE of PM for the emissions unit. 9 See: 1990 New Source Review Workshop Manual, DRAFT, at page B.5.

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5.2.6 BACT Technical Feasibility Criteria In the second step of a top-down BACT analysis, potentially available control strategies are evaluated for technical feasibility. A technically feasible control strategy is one that has been demonstrated to function efficiently on an emissions unit that is identical or similar to the emissions unit under review.10 For the purposes of assessing technical feasibility of an add-on control technology, the determination of whether an emissions unit should be considered to be identical or similar is usually based on the physical and chemical characteristics of the gas stream to be controlled. An add-on control technology applicable to one emissions unit may not be technically feasible for application to an apparently similar unit depending on differences in physical and chemical gas stream characteristics, and rejection of a control option based on technical infeasibility for BACT purposes is appropriate if “it is uncertain the control device will work in the situation currently undergoing review.”11 For control strategies that are not demonstrated, the analysis of technical feasibility is somewhat more involved. Two key concepts are important in determining whether an undemonstrated technology is feasible: “availability12” and “applicability.” A technology is considered “available” if it can be obtained by the applicant through commercial channels or is otherwise available within the common sense meaning of the term. An available technology is “applicable” if it can reasonably be installed and operated on the source type under consideration. A technology that is both available and applicable is technically feasible.

5.3 HBI Process Overview The HBI production process core plant consists of two main processes, a reformer and the DRI reactor (reduction furnace). The reformer produces the reducing gases (mainly H2 and CO) used to reduce iron oxide to a more pure metalized iron in the DRI reactor. The reformer is a proprietary tubular style design where natural gas feedstock disassociates to form a reducing gas rich in H2 and CO. The reducing gas removes oxygen from the oxide pellets. Floor-fired (burners are installed on the floor) main burners that are located on the bottom of the reformer box between tube rows and between the outside tube rows and the reformer wall provide heat for the reforming reactions. Preheated air for combustion in the burners is provided by the heat recovery system by the main air blower. The reformer box is lined by refractory material. Natural gas-fired auxiliary burners are utilized to both bring the plant up to operating temperature during startup and to maintain the temperature in reformer box during plant idle situation to reduce both restart time and thermal cycling of the reformer tubes.

10 See, Prevention of Significant Deterioration Workshop Manual, EPA-450/2-80-081, October 1980, at pp. I-B-6

through I-B-7. 11 See, PSD and Title V Permitting Guidance for Greenhouse Gases, EPA-457/B-11-001, March 2011, at p. 34. 12 In Step 2 of a top-down BACT analysis, the term “availability” has a different meaning than the term “available” in Step 1. Control strategies that are not “available” in Step 1 are not considered in Step 2.

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Uniform heat distribution along the reformer length is ensured by use of separate sized flue gas port for each flue gas header in the reformer bays. The flue gas headers are refractory lined and expansion joints are provided between the single sections of the headers to compensate for thermal expansion. Waste heat recovery system recovers the heat from the flue gas exiting the reformer via the flue gas headers. In the reduction furnace, the reducing gas is supplied from the tuyers located in the bottom of the reactor. Oxide is charged from the top of the reactor. Inert seal gas, that is cooled flue gas from the reformer, is used for sealing the top of the furnace. Seal gas escapes through the charge hopper as the charge hopper discharges oxide into the furnace. The gas flow is counter current to the descending oxide. MIDREX’s novel ACT system increases the CO concentration in the transition zone of the furnace allowing for the addition of more natural gas at higher temperatures in order to impart higher carbon to the DRI/HBI product. At the top of the reactor, the partially spent reducing gas exits and it is recompressed, enriched with natural gas, preheated, and transported back to the reformer (“top gas”). The top gas is reformed in the reformer to 95% H2 and CO, which is then reused in the reactor. A portion of the top gas is mixed with natural gas as fuel for use in the reformer burners. The DRI material is discharged from the reactor via a dynamic seal leg and a hydraulically driven variable speed hot wipe bar. The bottom seal gas (nitrogen) is vented through a vent line that is collected in a dilution hood. The speed of the lower burden feeder is closely ratioed to the average discharge rate of the reactor to achieve a uniform flow of the material from the lower cone to lower seal leg. The hot DRI material flows across the wiper bar and then passes through a set of hydraulically driven enclosed screens that limit the size of the product passing into the surge hopper of the product discharge chamber. The material is discharged from the surge hopper into one or more feed legs. These feed legs connect to briquette machine to produce HBI or the bypass feed screw for preventing off-spec material, i.e. remet, from reaching the briquette machine. In order to prevent the reducing gas from escaping the reduction furnace, high pressure seal gases are applied to both the charging and discharging openings. The seal gas escapes from the opening during oxide charge and product discharge from the furnace while retaining the reducing gas. The fines generated from oxide passing through the furnace escape along with seal gas. Top seal gas will be a small amount of flue gas (products of combustion) from the reformer exhaust. For bottom seal gas IU is planning to use nitrogen gas in place of cooled reformer flue gas, significantly reducing CO generation at this location. IU is the only facility in the world to primarily utilize nitrogen gas for the bottom seal. Other MIDREX facilities use seal gas for the bottom seal and only use nitrogen gas as an emergency back-up if sufficient seal gas is not available. The reduction furnace runs as close to steady state operations as possible to produce HBI of consistent and acceptable quality. Due to the nature of the reducing gas cycle system, during process upset or burden shift conditions, the pressure of reducing gas must be maintained below that of the seal gas system. This will prevent release of uncombusted reducing gases directly to the atmosphere from top and/or bottom seal. During these conditions reducing gases are routed to the pressure relief vent (flare) for flaring. Also during the process startup and shutdown

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events, the reducing gases are routed to the flare. The flare prevents release of carbon monoxide from the system by combusting the reducing gases and uses a natural gas fired pilot flame to ensure ignition of reducing gases. The required direct contact process water comes in contact with the process gases during the cooling process. Some of the gas constituents, mostly CO, is dissolved in water at elevated pressure in the system. As a safety precaution to minimize fugitive CO emissions at the clarifier and to reduce scaling in process water ducts, a forced degassing system will be used. The return water flow from the top gas scrubber weir (after depressurization) will be routed to a degasser vessel. Air will flow upwards, countercurrent to the down flowing hot return water in this vessel, releasing majority of dissolved CO. CO emissions are collected in the degasser vent gas flow and safely released to the atmosphere.

5.4 Oxide Handling Systems (Enclosed) PM/PM10/PM2.5 BACT Analysis

This section presents the required PM/PM10/PM2.5 BACT analyses for the enclosed iron ore pellets (oxide) handling operations. The enclosed oxide handling points include the following:

(a) Transfer of oxide from one conveyor to another. (b) Transfer of oxide to lumps screen to three oxide day bins. (c) Oxide day bins to conveyors. (d) Conveyors to screens. (e) Screening transfers.

5.4.1 PM/PM10/PM2.5 BACT Baseline There are no state, local or federal regulations applicable to PM/PM10/PM2.5 emissions from the transfer and handling of iron ore pellets at a HBI Facility. Therefore, there is no “BACT baseline” for this operation.

5.4.2 Step 1 – Identify Available PM/PM10/PM2.5 Control Options A summary of the precedents from U.S. EPA’s RBLC database and other known permit precedents for the enclosed oxide handling operations is presented in Table 5-3.

Table 5-3. Summary of PM/PM10/PM2.5 BACT Precedence for Oxide Handling RBLC ID/ State Facility Name Permit Date Process Description Control Emission Limit

gr/dscf

IN-0185 Mag Pellet LLC 4/24/2014 Oxide pellet loadout system Baghouses 0.0020

TX-0725 Voestalpine Texas DRI facility 3/18/2014 Oxide pellet transfer and dedusting Baghouses 0.0020

IN-0167 Magnetation LLC 4/16/2013 Oxide pellet storage and unloading system Baghouse 0.0020

MN-0085 Essar Steel Minnesota LLC 5/10/2012 Pellet screening and handling Baghouse 0.0020

LA-0248 Consolidated Environmental DRI facility (never built) 1/27/2011 Iron oxide day bins Baghouse 0.0020

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The oxide handling and screening operations result in release of small amount particulate matter emissions. The potential control options for controlling emissions from the oxide are identified below:

(a) Fabric filter (baghouse) (b) Electrostatic precipitator (ESP) (c) Venturi scrubber (d) Cyclone (e) Wet suppressions (f) Enclosures

Some of the control options listed here are described in the reformer section. Wet suppression and enclosures are described below. Wet Suppression – This technology involves use of fine mist of water to reduce particle generation from material handling operations. The wetted material becomes heavier and quickly settles reducing air borne emissions. Wet suppression may also increase moisture content and reduce emissions. Enclosures – Enclosures or covers are used for conveyor systems to prevent dust particles from entraining in the air stream including at various conveyor drop points to another conveyor or handling equipment.

5.4.3 Step 2 – Eliminate Technically Infeasible PM/PM10/PM2.5 Controls All of the identified control technologies are technically feasible for the enclosed oxide handling operations. Use of enclosure here represents the baseline case.

5.4.4 Step 3 – Rank PM/PM10/PM2.5 Control Options The particulate matter control strategies selected for the proposed enclosed oxide handling operations that are considered technically feasible and associated control efficiencies are:

(a) Baghouse – 99.9% (b) ESP – 99.5% (c) Venturi scrubber – 99% (d) Enclosure or hoods – ~95% (e) Wet suppression - 95% (f) Cyclones – 80%

5.4.5 Step 4 – Evaluate Feasible PM/PM10/PM2.5 Control Options The oxide handling operations that are to be enclosed will be exhausted to various baghouses as shown in Appendix B. Use of baghouse is the top control technology and will not have any material adverse energy, environmental or economic impacts. Therefore, it is appropriate that use of baghouses form the basis for establishing the PM/PM10/PM2.5 BACT limits for the proposed equipment.

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5.4.6 Step 5 – Establish PM/PM10/PM2.5 BACT The use of baghouse represents the top ranked control option for the oxide handling operations with enclosures. The combined PM10 and combined PM2.5 emissions from MTR-5, TR-1, TR-6, TR-7, TR-10, SR-1, TR-13a, TR-13b, and TR-14 shall not exceed 1.27 pounds per hour (each). Compliance with these limits will be demonstrated by meeting the equipment design specifications as noted in Appendix B and regular inspection and monitoring of the control devices. IU’s proposed PM/PM10/PM2.5 BACT limitations are based on the outlet grain loading information provided by the baghouse equipment supplier. Due to lack of testing requirements for the lower PM/PM10/PM2.5 grain loading rates in Table 5-3 above, we were unable to confirm whether the equipment was able to comply with the lower rates included in pre-construction permits and, therefore, we did not consider these unverified lower rates as PM/PM10/PM2.5 BACT limitations for these operations.

5.5 Oxide Transfers (open) Operations PM/PM10/PM2.5 BACT Analysis

This section presents the PM/PM10/PM2.5 BACT analysis for the open oxide transfer operations designed to occur outside of building enclosures. The open oxide transfer points include the following:

(a) Transfer of oxide to and from conveyors to stacker/reclaim machine. (b) Transfer of oxide to and from stacker/reclaim machine to and from oxide stockpiles. (c) Transfer of oxide lumps, fines, feed recovery, REMET from conveyors to stockpiles. (d) Transfer of oxide lumps, fines, feed recovery, REMET from front end loaders (FEL)

reclaim to truck/hopper.

5.5.1 PM/PM10/PM2.5 BACT Baseline There are no state, local or federal regulations applicable to PM/PM10/PM2.5 emissions from the open transfer and handling of iron ore pellets. Therefore, there is no “BACT baseline” for this operation.

5.5.2 Step 1 – Identify Available PM/PM10/PM2.5 Control Options The oxide handling operations result in release of a small amount particulate matter emissions. The potential control options for controlling emissions from the open oxide transfer operations are identified below:

(a) Fabric filter (baghouse) (b) Electrostatic precipitator (ESP) (c) Venturi scrubber (d) Cyclone (e) Water or chemical suppressants (f) Enclosures (g) Windshield

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5.5.3 Step 2 – Eliminate Technically Infeasible PM/PM10/PM2.5 Controls The open transfer of oxide and other materials by definition results in particulate matter emissions that are fugitive. As previously discussed in the prior PTI application, use of a building enclosure is infeasible and unreasonable for these operations. OAC 3745-31-01(UU) defines fugitive emissions as “…those emissions that cannot reasonably pass through a stack, chimney.” Since these operations occur in open areas by design, it is unreasonable to capture emissions from these open transfers. Therefore, add-on control technologies (baghouse, ESP, scrubber, cyclone) are not technically feasible for these operations. In addition, due to specific nature of the operations, i.e. mobile equipment such as stacker/reclaim machine, FEL etc., use of hoods or capture system is also not technically feasible. For materials transfers from the proposed FELs to either trucks or hopper, addition of water sprays is not feasible due to mobile nature of the equipment.

5.5.4 Step 3 – Rank PM/PM10/PM2.5 Control Options The particulate matter control strategies selected for the proposed open transfer of oxide and other materials that are considered technically feasible and associated control efficiencies are use of water or chemical suppressants at 95% control efficiency.

5.5.5 Step 4 – Evaluate Feasible PM/PM10/PM2.5 Control Options As shown in Appendix B, the open oxide transfer points will use water or chemical suppressants or windshields (in case of REMET pile) to control fugitive PM/PM10/PM2.5 emissions. Use of these controls are the top control technologies and will not have any material adverse energy, environmental or economic impacts. Therefore, it is appropriate that use of water or chemical suppressants or windshields form the basis for establishing the fugitive PM/PM10/PM2.5 BACT requirements for the proposed open oxide and REMET transfer equipment.

5.5.6 Step 5 – Establish PM/PM10/PM2.5 BACT Equipment design or work practice requirements are acceptable under the definition of BACT when technological or economic limitations on the application of measurement methodology would make the imposition of an emissions standard infeasible. That criterion is met with respect to particulate matter emissions from the open oxide transfer operations. The use of water or chemical suppressants or windshields represents the top ranked control option for the open oxide, lumps, fines, and REMET transfer operations and is BACT for fugitive PM/PM10/PM2.5 emissions from these operations.

5.6 Shaft Furnace Bottom Seal Gas Exhaust CO Analysis This section presents the required CO BACT analysis for the exhaust from the bottom seal gas of the shaft furnace. As previously noted in subsection 2.5, MIDREX collected additional stack testing information from the existing MIDREX facilities and updated their proprietary emission prediction model to account for additional CO generation that occurs from ongoing solid state carbon reactions from FeO in the hot product as it reacts with carbon; combustion of DRI fines in the bottom seal gas; and iron oxide feed variability.

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As part of the equipment design, IU is proposing to use nitrogen gas for the bottom seal gas in the shaft furnace. This will minimize CO emissions from the bottom seal gas exhaust.13

5.6.1 CO BACT Baseline There are no state, local or federal regulations applicable to CO emissions from the shaft furnace bottom seal gas exhaust. Therefore, there is no “BACT baseline” for this operation.

5.6.2 Step 1 – Identify Available CO Control Options A review of recent permit actions and search of U.S. EPA’s RBLC database did not reveal any application of CO add-on controls for the shaft furnace bottom seal gas exhaust at DRI/HBI facilities with or without ACT. For a similar operation listed as “Furnace Dedusting (BSG Dust Collection) Wet Scrubber Stack” at the Voestalpine Texas LLC (RBLC ID: TX-0785) facility, CO BACT limit is set at 873 lb/hour. The control is listed as “Good work practices and proper maintenance of gas reformer” as this facility uses reformer flue gas that is high in CO2 concentration as the seal gas for the bottom seal in the shaft furnace. However, the Voestalpine Texas LLC facility is not comparable to the IU Project as it does not employ the ACT system to adjust the carbon content. The ACT system allows IU to produce high carbon DRI/HBI to meet market requirements. MIDREX has determined that use of the ACT system to increase the carbon content of the DRI/HBI is the most significant driver of increased CO generation. MIDREX estimated CO emission rate of 2,906 lb per hour from the bottom seal gas exhaust if the system used the cooled reformer flue gas as seal gas. Based on the information from MIDREX, use of nitrogen as the seal gas in the product discharge chamber (PDC) of the shaft furnace and optimum equipment design is the only CO minimization strategy available for the bottom seal gas exhaust.

5.6.3 Step 2 – Eliminate Technically Infeasible CO Control Options Use of nitrogen as the seal gas in the PDC and optimum equipment design is the only feasible option for control of CO emissions from the bottom seal gas exhaust.

5.6.4 Step 3 – 5 Bottom Seal Gas Exhaust BACT for CO The most effective control strategy for CO emissions from the bottom seal gas exhaust is the use of nitrogen as the seal gas and use of optimum equipment design for the shaft furnace using ACT. No additional controls are feasible for the bottom seal gas exhaust. Since there are no add-on controls considered BACT for the bottom seal gas exhaust, IU proposes nitrogen gas and optimum equipment design as CO BACT for the shaft furnace bottom seal gas exhaust. IU’s proposal for CO emission limit for the bottom seal gas exhaust stack is 986.03 pounds per hour

13 Use of the reformer exhaust flue gases in the bottom seal gas system would bring the CO2 rich gases in contact with the hot DRI. The hot DRI, in the bottom of the shaft furnace, will strip some of the oxygen from CO2 in the flue gases used as seal gas forming CO and Fe2O3. This results in the generation of CO emissions from the bottom seal gas exhaust when reformer exhaust gases are used as seal gas. IU is not planning to use the reformer exhaust flue gases, except for abnormal situations, and instead use the nitrogen gas as seal gas in the bottom seal gas system of the shaft furnace. (explanation provided by the MIDREX representative)

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on a three-hour block average basis. Compliance with this limit will be demonstrated by conducting a performance test and operating in accordance with vendor recommendations.

5.7 Bottom Seal Gas Exhaust GHG Analysis The DRI reactor or shaft furnace uses the reducing gas generated by the reformer to react with iron ore to form metallized reduced iron. The DRI reactor, which does not involve combustion, reacts CO and H2 to scavenge oxygen from the ore pellets, reducing the oxygenation state of the ore. This results in pure iron, CO2, and water from the following reactions.

Fe2O3 + 3 CO → 2 Fe + 3 CO2 Fe2O3 + 3 H2 → 2 Fe + 3 H2O

Reducing gases from the reformer (rich in CO (5%) and H2 (95%)) enter at the bottom of the DRI reactor and ore pellets are fed from the top. As the reduction reaction occurs, CO2 and water vapor are formed in the gas stream as reaction byproducts. The spent reducing gases then exit from the top of the furnace for recycle to the reformer after undergoing cleaning and cooling in the system. A portion of clean top gas, enriched with natural gas, is routed as fuel to the reformer burners. The remaining clean top gas is compressed mixed with natural gas to form feedstock for the reformer (after preheating). The reformer produces reforming gases for re-use in the DRI reactor. The portion of seal gas and small amount of reducing gas generated in the furnace, which is released through bottom seal gas and hot briquette exhausts, contain small amount of GHGs. This section presents the required GHG BACT analysis for the bottom seal gas exhaust from the shaft furnace. As previously noted, as part of the equipment design, IU is proposing to use nitrogen gas as seal gas for the bottom seal gas in the shaft furnace. This will also minimize GHG emissions from the bottom seal gas exhaust.

5.7.1 GHG BACT Baseline There are no state, local or federal regulations applicable to GHG emissions from the bottom seal gas exhaust. Therefore, there is no “BACT baseline” for this operation.

5.7.2 Step 1 – Identify Available GHG Control Options A review of recent permit actions and search of U.S. EPA’s RBLC database did not reveal any application of add-on controls for the shaft furnace bottom seal gas exhaust at DRI/HBI facilities with or without ACT. Operational strategies for mitigation of GHG emissions is the use of nitrogen seal in the PDC and optimum equipment design for the bottom seal gas in the shaft furnace.

5.7.3 Step 2 – Eliminate Technically Infeasible GHG Control Options Use of nitrogen as the seal gas in the PDC and optimum equipment design are the only feasible option for control of GHG emissions from the bottom seal gas exhaust.

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5.7.4 Step 3 – 5 Bottom Seal Gas Exhaust BACT for GHG The most effective control strategy for GHG emissions from the bottom seal gas exhaust is the use of nitrogen as the seal gas in the PDC and optimum equipment design for the shaft furnace. No additional controls are feasible for the GHG emissions from this operation. Since there are no add-on controls considered BACT for the bottom seal gas exhaust, IU proposes optimum equipment design along with use of nitrogen seal gas as GHG BACT for the shaft furnace bottom seal gas exhaust.

5.8 Hot Briquette Machine Exhaust CO Analysis This section presents the required CO BACT analysis for exhaust from the hot briquette machine that compresses DRI to make HBI. As explained in subsection 2.5, MIDREX collected additional emissions data from the existing MIDREX facilities and updated their proprietary emission prediction model to account for additional CO generation that occurs from ongoing solid state carbon reactions from FeO in the hot product as it reacts with carbon; combustion of DRI fines in the hot briquette machine exhaust; re-oxidation of fines and chips at the briquette machine; and compression of DRI pores which contain residual CO.

5.8.1 CO BACT Baseline There are no state, local or federal regulations applicable to CO emissions from the hot briquette machine exhaust. Therefore, there is no “BACT baseline” for this operation.

5.8.2 Step 1 – Identify Available CO Control Options A review of recent permit actions and search of U.S. EPA’s RBLC database did not reveal any application of CO add-on controls for the hot briquette machine exhaust at DRI/HBI facilities with or without ACT. Therefore, use of optimum equipment design is the only control option for this operation.

5.8.3 Step 2 – Eliminate Technically Infeasible CO Control Options Use of optimum equipment design is the only feasible option for control of CO emissions from this exhaust.

5.8.4 Step 3 – 5 Hot Briquette Machine Exhaust BACT for CO The most effective control strategy for CO emissions from the hot briquette machine exhausts is the use of the optimum equipment design for this operation. No additional controls are feasible for the CO released from this operation. Since there are no add-on controls considered BACT for the hot briquette machine exhaust, IU proposes optimum equipment design as CO BACT for the hot briquette machine exhaust. IU’s proposal for CO emission limit for the hot briquette machine exhaust stack is 912.01 pounds per hour on a three hour block average basis. Compliance with this limit will be demonstrated by conducting a performance test and operating in accordance with vendor recommedations.

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5.9 Briquette Cooling System Vapor Removal Vent CO Analysis

This section presents the required CO BACT analysis for the exhaust from the briquette cooling system vapor removal vent. The HBI cooling system sprays water to cool the HBI product. Steam and vapor from the process are cooled and exhausted to the atmosphere by a hood. This emissions point will be equipped with venturi scrubber to control particulate matter emissions from release of seal gas. The exhaust released here contains CO that will be emitted to the atmosphere. As explained in subsection 2.5, MIDREX collected additional information from the existing MIDREX facilities and updated their proprietary emission prediction model to account for additional CO generation that occurs from re-oxidation of fines and chips along the briquette cooling conveyor and for cooling water sprays which can react with carbon in the hot HBI product to form CO.

5.9.1 CO Baseline There are no state, local or federal regulations applicable to CO emissions from the briquette cooling system vapor removal vent. Therefore, there is no “BACT baseline” for this operation.

5.9.2 Steps 1 - 3 – CO Control Options A review of recent permit actions and search of U.S. EPA’s RBLC database did not reveal any application of CO add-on controls for the vapor removal vent at DRI/HBI facilities. The low concentration of CO at this emission point and the presence of water in the exhaust make add-on controls e.g., oxidation catalysts for CO removal technically infeasible and cost ineffective.

5.9.3 Step 4 - 5 – Establish CO BACT The most effective control strategy for CO emissions from the vapor removal vent is the use of optimum equipment design. There are no other MIDREX technology that uses add-on controls. Since there are no add-on controls considered BACT for the vapor removal vent at DRI/HBI facilities with or without ACT, IU proposes optimum equipment design as CO BACT for this vent. IU’s proposal for CO emission limit for the vapor removal vent stack is 594.1 pounds per hour on a three hour block average basis. Compliance with this limit will be demonstrated by conducting a performance test and operating in accordance with vendor recommendations.

5.10 Degasser Exhaust CO and GHG BACT Analyses This section presents the required CO and GHG BACT analyses for the process water degasser exhaust. Due to the direct contact of process water with process gases (especially top gas), some gas constituents (especially CO and CO2) are dissolved in water at an elevated process gas pressure and temperature. The dissolved CO and CO2 is stripped in the degasser using pressurized air prior to the clarifier. As explained in subsection 2.5, MIDREX updated their CO emissions for this exhaust to account for maximum CO and CO2 solubility in water at 1 atm and 80 degrees Celsius (CO = 0.01 g CO/kg water; CO2 = 0.45 g CO2/kg water)

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5.10.1 Degasser Exhaust CO BACT Analysis CO is stripped from the cooling water prior to entering the clarifier. CO BACT analysis for the degasser exhaust is addressed in this section.

5.10.1.1 CO BACT Baseline There are no state, local or federal regulations applicable to CO emissions from the degasser exhaust at DRI/HBI facilities. Therefore, there is no “BACT baseline” for this operation.

5.10.1.2 Step 1 – Identify Available CO Control Options A review of recent permit actions and search of U.S. EPA’s RBLC database did not reveal any application of CO add-on controls for degassers at DRI/HBI facilities with or without ACT. The following list of controls that have been used to control CO emissions from process water stripper streams at other facilities in general.

• Optimum equipment design and operating practices • Flare

5.10.1.3 Step 2 – Eliminate Technically Infeasible CO Control Options Combustion of stripped CO in a flare or similar combustion devices is potentially applicable for this operation. However, the concentration of CO is only 0.17% of the exhaust stream. On the other hand, water/moisture content of the exhaust stream is approximately 26%. In addition, the CO concentration in the exhaust stream fluctuates based on air and water flows in the degasser. Use of a flare on this type of operation with low CO concentration and high moisture is not technically feasible.

5.10.1.4 Step 3 – 5 Degasser Exhaust BACT for CO The most effective control strategy for CO emissions from the degasser exhaust is the use of optimum equipment design. No additional controls are feasible for the CO emissions from stripping of process water stream. Equipment design or work practice requirements are acceptable under the definition of BACT when technological or economic limitations on the application of measurement methodology would make the imposition of an emissions standard infeasible. That criterion is met with respect to CO emissions from the degasser exhaust. Since there are no add-on controls considered BACT for the degasser exhaust, IU proposes optimum equipment design as BACT for CO from the degasser exhaust.

5.10.2 Degasser Exhaust GHG BACT Analysis Along with CO, some of the CO2 is also stripped from the cooling water prior to entering the clarifier. CO2 BACT analysis for the degasser exhaust is addressed in this section.

5.10.2.1 GHG BACT Baseline There are no state, local or federal regulations applicable to GHG emissions from the degasser exhaust from DRI/HBI facilities. Therefore, there is no “BACT baseline” for this operation.

5.10.2.2 Step 1 – Identify Available GHG Control Options A review of recent permit actions and search of U.S. EPA’s RBLC database did not reveal any

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application of CO2 add-on controls for degassers at DRI/HBI facilities with or without ACT. The following list of controls have been used for process water stripper streams at other facilities in general.

• Caustic/water wash scrubber – A caustic/water scrubber can be used to remove CO2 from the process water degasser exhaust. In addition, production of caustic soda (NaOH) will result in generation of off-site GHG emissions both from energy use as well as from chemical reaction.

• Optimum equipment design and operating practices – These include appropriate equipment design and maintenance within the operational parameters for minimizing emissions.

5.10.2.3 Step 2 – Eliminate Technically Infeasible GHG Control Options Use of caustic/water wash scrubber for the small amount of CO2 in the process water degassing operation is generally considered technically infeasible. However, for purposes of this analysis, IU evaluated this control as part of the BACT.

5.10.2.4 Step 3 – Rank Remaining GHG Control Strategies Application of caustic/water scrubber can remove almost 99% of CO2 depending upon the type of reagent used.

5.10.2.5 Step 4 – Evaluate Remaining GHG Control Strategies Although technically feasible, use of a caustic/water scrubber to control the small amount of CO2 emissions that occur from process water degassing is likely to be cost prohibitive. Caustic soda prices ranged from $400 to $600 per ton.14 Since CO2 removal requires caustic soda use at the rate of at least 1:1 molar ratio, the cost effectiveness of this option will be at least $400 per ton of CO2 removed. Process water degassing operation emits very small amount (approximately 18,000 tons per year or 1.1% of site-wide CO2e emissions). Due to the unreliability of operation, small potential CO2 reductions, and high cost of reagent used, this technology is deemed cost prohibitive.

5.10.2.6 Step 5 – Establish GHG BACT The most effective control strategy for CO2 emissions from the degasser exhaust is the use of optimum equipment design and operation. No additional controls are feasible for the CO2 emissions from stripping of process water stream. Equipment design or work practice requirements are acceptable under the definition of BACT when technological or economic limitations on the application of measurement methodology would make the imposition of an emissions standard infeasible. Since there are no add-on controls considered BACT for the degasser exhaust, IU proposes optimum equipment design and operation as BACT for GHGs from the degasser exhaust.

14 Prices checked on 8/3/2017: https://www.alibaba.com/showroom/sodium-hydroxide-price.html

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5.11 Pressure Relief Vent/Flare NOx, CO, and GHG BACT Analyses

This section presents the required NOx, CO, and GHG BACT analysis for the proposed flare. Top gas combustion in the flare and natural gas combustion in the pilot results in formation of products of combustion. However, other than the flare pilot, the emissions occur on intermittent basis during process upsets, startup, and shutdown.

5.11.1 NOx, CO, GHG BACT Baselines There are no state, local or federal regulations applicable to NOx, CO, GHG emissions from the proposed flare. Therefore, there is no “BACT baseline” for this operation.

5.11.2 Step 1 – Identify Available NOx, CO, GHG Control Options The identified control options for minimizing emissions from the flare are work practices and equipment design elements that will minimize use of the flare and will minimize emissions from the flare during flaring events:

• Minimizing the combustion process gas to be flared by modifying startup and shutdown procedures;

• Designing the flare to meet limitations on maximum exit velocity; and • Designing the flare to meet minimum net heating values.

Each of these control options is technically feasible and is inherent in the design of the proposed flare. Other controls used for gas combustion devices include:

• Good combustion practices; • Oxidation catalyst for CO control; and • LNBs and SCR for NOx control.

These controls are already described in the reformer exhaust BACT analysis presented earlier in this section.

5.11.3 Step 2 – Eliminate Technically Infeasible NOx, CO, GHG Controls Good combustion practices (GCP), is considered technically feasible and is the only control identified as BACT for flares. Add-on controls such as oxidation catalyst and SCR are not technically feasible due to the high combustion temperatures and the intermittent use of the flare for combusting process gas during process upset/startup/shutdown.

5.11.4 Step 3 – 5 Flare BACT for NOx, CO, GHG The most effective control strategy for NOx, CO, and GHG emissions from the flare are the work practices and equipment design elements identified above. Establishment of equipment design and work practice requirements as BACT is appropriate in this instance because it is infeasible to apply a measurement methodology for demonstration of compliance with numeric limits on emissions rates. The configuration of the elevated flare renders both manual stack

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testing and continuous emissions monitoring systems technically infeasible. IU proposes the following equipment design and work practices.

• The HBI process will minimize flaring resulting from startups, shutdowns, and upset events by operating at all times in accordance with an approved flare minimization plan. The plan shall include the following elements:

o Procedures for operating and maintaining the flare during periods of startup, shutdown, and process upset.

o A program of corrective action for malfunctioning equipment in the HBI process. o Procedures to minimize discharges to the flare gas system during the planned and

unplanned startup or shutdown of HBI process plant equipment. • The flare shall be designed to meet limitations on maximum exit velocity, as set forth in

the NSPS general provisions at 40 CFR § 60.18. The flare shall be designed to meet minimum net heating value requirements for fuel gas combusted in the flares, as set forth at 40 CFR § 60.18.

5.12 Emergency Engines BACT Analyses The Project revision will include increased output for the emergency fire water booster pump engine and one Administrative Building emergency engine generator. These emergency equipment will be powered by compression-ignition reciprocating internal combustion engines (i.e., a diesel fueled RICE) with a rated output of 311 brake horsepower (“bhp”) for the fire water booster pump and 133 bhp for the Administrative Building emergency generator.15 These engines are generally similar to engines that are regulated as non-road mobile engines under 40 CFR parts 89 and 1039. These engines are subject to BACT review for PM/PM10/PM2.5, NOx, CO, and GHG emissions.

5.12.1 Emergency Engines PM/PM10/PM2.5 BACT Analysis

5.12.1.1 PM/PM10/PM2.5 BACT Baseline As discussed in Section 4 herein, the emergency engines will be affected facilities subject to the standards for RICE under subpart IIII of 40 CFR part 60. The minimum standards that would meet BACT requirements for particulate matter emissions from these engines are as follows:

• The fire water pump booster engine, pursuant to 40 CFR § 60.4205(c), will be required to meet the PM emission standard established for nonroad engines of the same model year pursuant to Table 4 of subpart IIII. The PM emission standard is a specification of 0.15 g/bhp-hr, as determined by the engine manufacturer using the nonroad engine testing procedures set forth at 40 CFR §§ 89.401 to 89.424 and at Table 4 of subpart IIII.

• The emergency generator engine, pursuant to 40 CFR § 60.4205(b), will be required to meet the PM emission standard established for nonroad engines of the same model year 40 CFR § 60.4202. Per 40 CFR §60.4202(b)(2), specific limitations in 40 CFR §§ 89.112 and 89.113 are applicable to the emergency engine that is not a fire pump. The PM

15 There is another emergency generator (2,700 bhp) for the process. There is no change to that unit.

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emission standard is a specification of 0.30 g/kW-hr, as determined by the engine manufacturer using the nonroad engine testing procedures set forth at 40 CFR §§ 89.401 to 89.424.

5.12.1.2 Steps 1 – Identify Available Control Options Identified control technologies and techniques for PM/PM10/PM2.5 emissions from compression-ignition RICE include the following:

• Engine manufacturer certification for NSPS, injection timing retard, also called ignition timing retard, which involves delaying the fuel injection point in each engine cycle such that the heat release from fuel combustion occurs during the cylinder expansion. Lower NOX emissions are achieved by reducing the peak combustion temperature;

• An oxidation catalyst for control of organics, similar to the catalyst described in earlier sections; and

• Catalyzed diesel particulate filters, which control emissions by capturing particulate matter in a filter media, typically a ceramic wall flow substrate, and then by oxidizing it in the oxygen-rich atmosphere of diesel exhaust. The particulate matter emitted by diesel engines includes semi-volatile organic compounds that are regulated as VOC.

5.12.1.3 Step 2 – Eliminate Technically Infeasible Options All of the identified control options are assumed to be technically feasible.

5.12.1.4 Step 3 – Rank Feasible Control Options The third-ranked control option for particulate matter emissions comprise the use of internal combustion engines certified by the engine manufacturer to meet the applicable NSPS emission standards for non-road, compression-ignition engines. Engines meeting these standards may use multiple in-engine control technologies including injection timing retard and exhaust gas recirculation. These technologies will reduce VOC emissions from the engines resulting in lower reported PM emissions. The second-ranked control option for PM/PM10/PM2.5 emissions involves the use of oxidation catalyst in conjunction with the third-ranked control option. For the purposes of this BACT analysis, it is assumed that an 80 percent reduction in VOC emissions is achievable with this control option. This likely overstates the achievable emission reduction by a significant amount, as the engine will have very little time operating under the steady-state conditions favorable for oxidation catalyst system performance. The highest-ranked control option for PM/PM10/PM2.5 emissions involves the use of catalyzed diesel particulate filters in conjunction with the third-ranked control option. For the purposes of this BACT analysis, it is assumed that 90 percent emission reduction is achievable.

5.12.1.5 Step 4 – Evaluate Feasible Control Options Third-ranked control option, use of certified engines, will not cause any adverse energy, environmental, or economic impacts. The higher-ranked control options will cause adverse impacts that warrant their exclusion as the basis for establishing PM/PM10/PM2.5 BACT limits

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from the fire pump booster engine and the emergency generator engine. The adverse impacts include energy impacts, due to reduced energy efficiency attributable to increased pressure drop, and environmental impacts associated with catalyst disposal. These adverse energy and environmental impacts are minimal. The adverse economic impacts that would result from requiring catalytic add-on controls for an emergency use, internal combustion engine would be significant. Economic analyses prepared by U.S. EPA in its rulemaking for NSPS 40 CFR 60 Subpart IIII showed that, for emergency use engines, the cost of oxidation catalyst control and catalyzed diesel particulate filters are not cost effective.16 The 2005 rulemaking memorandum in the docket indicates oxidation catalyst cost effectiveness of over $100,000 per year of PM controlled and the cost of catalyzed diesel particulate filters and NOX adsorbers are more than $20,000 per ton of total NOX and VOC emission reduction.17 Considering the minimal environmental benefit that would result, and the adverse energy, economic and environmental impacts described above, these controls are rejected as BACT.

5.12.1.6 Step 5 – Establish BACT The fire pump booster engine and the emergency generator engine to be installed at the HBI Facility will be certified by the equipment manufacturer to meet the applicable emission standards for nonroad, compression-ignition engines, as codified in 40 CFR Part 60 Subpart IIII and at 40 CFR § 89.112. Due to the very low emissions from these engines, the fact that these will operate only intermittently, that non-emergency use operation is limited to 100 hours per year, and the availability of engines that are certified to achieve this emission level, and considering the nature of the certification test procedure for the nonroad engine emission standards, IU proposes that an equipment design standard rather than an emission rate limit is an appropriate form of expression for the PM/PM10/PM2.5 BACT requirements for the fire pump booster engine and the emergency generator engine.

5.12.2 Emergency Engines NOx BACT Analysis

5.12.2.1 NOx BACT Baseline As discussed previously, the emergency fire pump booster engine and the emergency generator engine will be affected facilities subject to the standards for emergency engines under 40 CFR Part 60 Subpart IIII. The minimum standards that would meet BACT requirements for NOX emissions from these engines are as follows:

• The fire water pump booster engine, pursuant to 40 CFR § 60.4205(c), will be required to

meet the NOx and non-methane hydrocarbons emissions standard established for nonroad engines of the same model year pursuant to Table 4 of subpart IIII. The emission standard is a specification of 4.0 g/bhp-hr, as certified by the engine manufacturer using the

16 70 Fed. Reg. 39870, July 11, 2005, page 39883. 17 Memorandum “Cost per Ton for NSPS for Stationary CI RICE,” from Tanya Parise, Alpha-Gamma Technologies Inc., June 9, 2005, EPA-HQ-OAR-2005-0029-0014.

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nonroad engine testing procedures set forth at 40 CFR §§ 89.401 to 89.424 and at Table 4 of subpart IIII.

• The emergency generator engine, pursuant to 40 CFR § 60.4205(b), will be required to meet the NOx and non-methane hydrocarbons emissions standard established for nonroad engines of the same model year 40 CFR § 60.4202. Per 40 CFR §60.4202 (b)(2), specific limitations in 40 CFR §§ 89.112 and 89.113 are applicable to the emergency engine that is not a fire pump. The emission standard is a specification of 4.0 g/kW-hr, as certified by the engine manufacturer using the nonroad engine testing procedures set forth at 40 CFR §§ 89.401 to 89.424.

5.12.2.2 Step 1 – Identify Available Control Options Identified control technologies and techniques for NOX emissions from compression-ignition RICE include the following:

• Injection timing retard, also called ignition timing retard, which involves delaying the fuel injection point in each engine cycle such that the heat release from fuel combustion occurs during the cylinder expansion. Lower NOX emissions are achieved by reducing the peak combustion temperature;

• Exhaust gas recirculation, which involves retaining or re-introducing a fraction of the exhaust gases. Lower NOX emissions are achieved by reducing the peak combustion temperature and by reducing the amount of available molecular oxygen;

• NOX adsorber technology, which typically utilizes alkali or alkaline earth metal catalysts to adsorb NOX on the catalyst surface under the fuel-lean and oxygen-rich conditions typical of diesel engine exhaust. Periodically, the catalyst bed is subjected to fuel-rich exhaust in order to desorb the NOX and regenerate the catalyst. The desorbed NOX is catalytically reduced over a second catalyst, typically platinum and rhodium; and

• SCR for NOX reduction.

5.12.2.3 Step 2 – Eliminate Technically Infeasible Options All of the identified control options are assumed to be technically feasible.

5.12.2.4 Step 3 – Rank Feasible Control Options The third-ranked control option for NOX emissions comprises the use of internal combustion engines certified by the engine manufacturer to meet the applicable NSPS emission standards for non-road, compression-ignition engines. Engines meeting these standards may use multiple in-engine control technologies including injection timing retard and exhaust gas recirculation. The second-ranked control option for NOX emissions involves the use of SCR in conjunction with the third-ranked control option. For the purposes of this BACT analysis, it is assumed that an 80 percent reduction in NOX emissions is achievable with this control option. This likely overstates the achievable emission reduction by a significant amount, as the engine will have very little time operating under the steady-state conditions favorable for SCR and oxidation catalyst system performance.

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The highest-ranked control option for NOX emissions involves the use of catalyzed diesel particulate filters and NOX adsorber technology in conjunction with the third-ranked control option. For the purposes of this BACT analysis, it is assumed that 90 percent emission reduction is achievable.

5.12.2.5 Step 4 – Evaluate Feasible Control Options Third-ranked control option will not cause any adverse energy, environmental, or economic impacts. The higher-ranked control options will cause adverse impacts that warrant their exclusion as the basis for establishing NOx BACT limits from the fire pump booster engine and the emergency generator engine. The adverse impacts include energy impacts, due to reduced energy efficiency attributable to increased pressure drop, and environmental impacts associated with catalyst disposal. These adverse energy and environmental impacts are minimal. The adverse economic impacts that would result from requiring catalytic add-on controls for an emergency use, internal combustion engine would be significant. Economic analyses prepared by U.S. EPA in its rulemaking for NSPS subpart IIII showed that, for emergency use engines, the cost effectiveness of SCR is more than $100,000 per ton of NOX reduction, and the cost of catalyzed diesel particulate filters and NOX adsorbers are more than $20,000 per ton of total NOX and VOC emission reduction.18 Considering the minimal environmental benefit that would result, and the adverse energy, economic and environmental impacts described above, these controls are rejected as BACT.

5.12.2.6 Step 5 – Establish BACT The fire pump booster engine and the emergency generator engine to be installed at the HBI Facility will be certified by the equipment manufacturer to meet the applicable emission standards for nonroad, compression-ignition engines, as codified in 40 CFR Part 60 Subpart IIII and at 40 CFR § 89.112. Subpart IIII also limits the operation of the emergency engines for non-emergencies to less than 100 hours per year. Due to the very low emissions from these engines, the fact that these will operate only intermittently, and the availability of engines that are certified to achieve this emission level, and considering the nature of the certification test procedure for the nonroad engine emission standards, IU proposes that an equipment design standard rather than an emission rate limit is an appropriate form of expression for the NOX BACT requirements for the fire pump booster engine and the emergency generator engine.

5.12.3 Emergency Engines CO BACT Analysis

5.12.3.1 CO BACT Baseline As discussed previously, emergency fire pump booster engine and emergency generator engine will be affected facilities subject to the standards for emergency engines under 40 CFR Part 60 Subpart IIII. The minimum standards that would meet BACT requirements for CO emissions from these engines are as follows:

18 Memorandum “Cost per Ton for NSPS for Stationary CI RICE,” from Tanya Parise, Alpha-Gamma Technologies Inc., June 9, 2005, EPA-HQ-OAR-2005-0029-0014.

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• The fire water pump booster engine, pursuant to 40 CFR § 60.4205(c), will be required to meet the CO emission standard established for nonroad engines of the same model year pursuant to Table 4 of subpart IIII. The emission standard is a specification of 2.6 g/bhp-hr, as certified by the engine manufacturer using the nonroad engine testing procedures set forth at 40 CFR §§ 89.401 to 89.424 and at Table 4 of subpart IIII.

• The emergency generator engine, pursuant to 40 CFR § 60.4205(b), will be required to meet the CO emission standard established for nonroad engines of the same model year 40 CFR § 60.4202. Per 40 CFR §60.4202 (b)(2), specific limitations in 40 CFR §§ 89.112 and 89.113 are applicable to the emergency engine that is not a fire pump. The emission standard is a specification of 5.0 g/kW-hr, as certified by the engine manufacturer using the nonroad engine testing procedures set forth at 40 CFR §§ 89.401 to 89.424.

5.12.3.2 Steps 1 – 4 – Evaluate Feasible Control Options Potentially available control technologies and techniques for CO emissions include the combustion controls identified as options for VOC (as PM) control in sub-section 5.12.1.2. All of these technologies are assumed to be technically feasible. The baseline control option, using the internal combustion engines certified by the engine manufacturer to meet the applicable NSPS emission standards for non-road, compression-ignition engines, will result in potential CO emissions of 0.45 tons per year from the fire pump booster engine and 0.27 tons per year from the emergency generator engine. The top-ranked control option - addition of an oxidation catalyst - may be able to achieve some CO emission rate reduction, but is rejected as BACT due to its adverse energy, environmental, and economic impacts and its minimal environmental benefit, as discussed in the engine PM BACT analysis.

5.12.3.3 Step 5 – Establish BACT The fire pump booster engine and the emergency generator engine to be installed at the HBI Facility will be certified by the equipment manufacturer to meet the applicable emission standards for nonroad, compression-ignition engines, as codified in 40 CFR Part 60 Subpart IIII and at 40 CFR § 89.112. Due to the very low emissions from these units, the fact that these will operate only intermittently, that non-emergency use operation is limited to 100 hours per year, and the availability of engines that are certified to achieve this emission level, and considering the nature of the certification test procedure for the nonroad engine emission standards, SRP proposes that an equipment design standard rather than an emission rate limit is an appropriate form of expression for the CO BACT requirements for the fire pump booster engine and the emergency generator engine.

5.12.4 Emergency Engines GHG BACT Analysis The fire pump booster engine and the emergency generator engine will result in GHG emissions from combustion of diesel fuel by the engines during those brief periods when these will operate. The GHG PTE, assuming 500 hours of operation per year for each engine, is 99 tons of CO2e per year for the fire pump booster engine and 39 tons per year for the emergency generator engine or about 0.0005% of the source-wide GHG PTE. The baseline emission level for these engines, representing proper equipment design and operation and the use of diesel fuel, is a GHGs

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emission factor of 163.6 lb/MMBtu of fuel burned. On a mass basis, emissions of CH4 and N2O comprise 0.005 percent of total GHG emissions from the engines, with the remainder being CO2.

5.12.4.1 GHG BACT Baseline There are no applicable NSPS or NESHAP rules that would establish a baseline emission rate for GHG emissions from the emergency engines.

5.12.4.2 Steps 1 – 4 – Evaluate Feasible Control Options The only identified control technologies for GHG emissions from the emergency diesel engines are oxidation catalyst (for control of CH4 emissions)19 and CCS (for control of CO2 emissions). Each of these technologies is assumed to be technically feasible. The use of oxidation catalyst could achieve some level of CH4 emission reduction, but is rejected as BACT due to its adverse energy, environmental, and economic impacts and its minimal environmental benefit, as discussed in the PM BACT analysis above. Similarly, CCS is rejected as BACT because it is infeasible, and even if feasible, would not be cost effective, as discussed in the GHG BACT discussion for the reformer.

5.12.4.3 Step 5 – Establish BACT No available control strategy more effective than the inherent engine design has been identified as BACT for GHG emissions from the fire pump booster engine and the emergency generator engine at the HBI Facility. Therefore, IU proposes that an emission limit of 163.6 lb/MMBtu of fuel burned be established for GHG emissions from these emergency engines, on a CO2e basis, with compliance to be demonstrated using the procedures of 40 CFR § 98.33 (as of August 4, 2017).

5.13 Equipment Leaks GHG BACT Analysis The Project revision corrects the original permit application’s estimated number of equipment components such as valves and flanges that supply natural gas to the HBI core plant. Some of the components have the potential to leak, resulting in fugitive emissions of natural gas containing CH4 which is a GHG with a global warming potential (GWP) of 25. This section presents the required GHG BACT analysis for equipment leaks associated with the natural gas supply system piping. Table 5-4 presents a revised estimate of the number of equipment components that have the potential to emit fugitive natural gas along with an estimate of the uncontrolled methane emissions from these components. Detailed emissions calculations are provided in Appendix B.

19 Oxidation catalyst will increase GHG emissions on a mass basis but due to the differing global warming potentials of CH4 and CO2, oxidation of CH4 is nonetheless considered a GHG control option.

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Table 5-4. PTE of CH4 from the Project Equipment Components Component Type Quantity CH4 PTE (tons/year)

Valves – Gas Service 418 23.45 Pressure Relief Valves – Gas Service 54 52.77 Connectors 1,982 34.08

Total Emissions = 110.29

5.13.1 GHG BACT Baseline There are no state, local or federal regulations applicable to the GHG emissions from the natural gas supply piping in the proposed Project. Therefore, there is no “BACT baseline” for this unit-pollutant group.

5.13.2 Step 1 – Identify Available Control Options The only potentially available control strategy identified to reduce fugitive emissions from equipment leaks is a leak detection and repair (LDAR) program. LDAR is a work practice that is commonly used in the petroleum refining and synthetic organic chemical manufacturing industry to reduce VOC emissions from equipment leaks. Such a program involves periodic monitoring to identify components with leak rates above a set threshold, and when such components are identified, efforts are made to repair the component and thereby reduce or eliminate leaks. There are no other available control options for reducing fugitive emissions from equipment leaks.

5.13.3 Step 2 – Eliminate Technically Infeasible Options The use of an LDAR program is a feasible means of reducing fugitive CH4 emissions from leaking components.

5.13.4 Step 3 – Rank Control Options The costs and effectiveness of LDAR programs vary according to the leak repair threshold selected. For purposes of this BACT analysis, it is assumed that leak repair thresholds equivalent to those required 40 CFR 63, subpart H would be utilized. On average, these thresholds are estimated to reduce emissions by 91% relative to the uncontrolled fugitive emissions from leaking components. This is the most effective feasible control option available to reduce fugitive CH4 emissions from the natural gas piping.

5.13.5 Step 4 – Evaluate Feasible Control Options Table 5-5 summarizes the costs and benefits of implementing an LDAR program on the planned Project to reduce fugitive CH4 emissions from natural gas piping leaks. As shown in the table, the costs of implementing such a program are excessive relative to the emissions reductions that would result. This table is based on the premise that a VOC control cost threshold of $20,000/ton is excessive. Crediting this cost threshold to the LDAR VOC emissions reductions results in a GHG emissions control cost (on a CO2e basis) of $1,040/ton. Detailed cost calculations are attached in Appendix C.

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5.13.6 Step 5 – Establish BACT A cost effectiveness of $39 per ton of CO2e results in unreasonable economic impacts. Thus, based on the excessive costs and limited benefits of implementing an LDAR program to reduce fugitive CH4 emissions from leaking components, IU concludes that it is unreasonable to require such a program as BACT for reducing fugitive emissions from the natural gas supply system. IU further concludes that BACT for fugitive CH4 emissions from leaking components is good industrial design coupled with routine operation and maintenance of the equipment consistent with the all applicable safety standards.

Table 5-5. Control Costs for Natural Gas LDAR Program20

Cost Category / Element Value Annualized Capital Costs - $/year (Annualized cost of capital required to establish LDAR program) $69,126

Annual O&M Costs - $/year (Annual direct and indirect costs to operate LDAR program) $105,336 Gross Annualized Costs - $/year $174,463 Amount of NG recovered (ton/year) 106.26 Amount of CH4 Controlled (T/yr) 103.39 Amount of VOC Controlled (T/yr) 2.86 Value of NG “recovered” $17,316 Credit for VOC @ $20,000 T $57,279 Total Net Annualized Costs $92,867 Cost Effectiveness ($/ton CO2e) $39

5.14 HBI Handling Systems (Enclosed) PM/PM10/PM2.5 BACT Analysis

This section presents the required PM/PM10/PM2.5 BACT analysis for the enclosed HBI handling systems. The enclosed HBI handling points include the following:

(a) Transfer of HBI from one conveyor to another. (b) Transfer of HBI to loadout bins. (c) HBI truck loadout building exhaust.

5.14.1 PM/PM10/PM2.5 BACT Baseline There are no state, local or federal regulations applicable to PM/PM10/PM2.5 emissions from the transfer and handling of HBI. Therefore, there is no “BACT baseline” for this operation.

20 LDAR costs and benefits estimated based on data in: Hazardous Air Pollutant Emissions from Process Units in

the Synthetic Organic Chemical Manufacturing Industry-Background Information for Proposed Standards - Volume 1C: Model Emission Sources, Emission Standards Division, U.S. Environmental Protection Agency, Office of Air and Radiation, Office of Air Quality Planning and standards, Research Triangle Park, North Carolina 27711, November 1992; EPA-453/D-92-016c. See Appendix C for additional details.

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5.14.2 Step 1 – Identify Available PM/PM10/PM2.5 Control Options A summary of the precedents from U.S. EPA’s RBLC database and other known permit precedents for the HBI handling is presented in Table 5-6.

Table 5-6. Summary of PM/PM10/PM2.5 BACT Precedence for HBI Handling RBLC ID/ State Facility Name Permit Date Process Description Control Emission Limit

gr/dscf

TX-0725 Voestalpine Texas DRI facility 3/18/2014 HBI cooling conveyors Wet scrubber 0.0079

HBI handling and screening systems result in release of small amount particulate matter emissions. The potential control options for controlling emissions from the HBI are identified below:

(a) Fabric filter (baghouse) (b) Electrostatic precipitator (ESP) (c) Venturi scrubber (d) Cyclone (e) Wet suppressions (f) Enclosures

5.14.3 Step 2 – Eliminate Technically Infeasible PM/PM10/PM2.5 Controls DRI particulates have high iron content. ESPs are especially sensitive to electrical resistivity, and iron particles adhere very strongly to the ESP collection plates. This makes it difficult to remove the iron particles, which quickly reduces ESP efficiency. Additionally, the application of an ESP creates a significant fire safety hazard when handling the captured DRI particles if exposed to air. The use of an ESP for cleaning the HBI handling exhaust is considered technically infeasible. As is the case for the use of ESP, the use of a cyclone for removal of DRI particles creates a significant fire safety hazard when handling the captured DRI particles. The use of a cyclone for cleaning the exhaust from HBI handling is considered technically infeasible. The use of either a venturi scrubber or a baghouse is considered technically feasible, as are wet suppressions and enclosures.

5.14.4 Step 3 – Rank PM/PM10/PM2.5 Control Options The particulate matter control strategies selected for the proposed enclosed HBI handling operations that are considered technically feasible and associated control efficiencies are:

(a) Venturi scrubber – 99% (b) Baghouse (where applicable) – 99% (c) Enclosure or hoods – ~95% (d) Wet suppression - 95%

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5.14.5 Step 4 – Evaluate Feasible PM/PM10/PM2.5 Control Options The HBI handling systems that are to be enclosed will be exhausted to various venturi scrubbers and baghouses (where applicable) as shown in Appendix B. DRI is formed in a reduced oxygen atmosphere, and its particles, when hot, are known to react to oxygen when exposed to the atmosphere. This exothermal reaction is known to cause fires. Therefore, baghouse is infeasible for controlling PM for hot HBI handling and transfer points and a scrubber is proposed for that application. Use of particulate matter control scrubbers and baghouses are the top control technologies and will not have any material adverse energy, environmental or economic impacts. Therefore, it is appropriate that use of scrubbers and baghouses form the basis for establishing the PM/PM10/PM2.5 BACT limits for the proposed equipment.

5.14.6 Step 5 – Establish PM/PM10/PM2.5 BACT The use of scrubbers and baghouses represents the top ranked control option for the HBI handling systems with enclosures. The combined PM10 and combined PM2.5 emissions from TR-17, TR-18, TR-23, TR-24, TR-25, and TR-28a shall not exceed 0.54 pounds per hour (each). Compliance with these limits will be demonstrated using by meeting the equipment design specifications as noted in Appendix B and regular inspection and monitoring of the control devices.

5.15 HBI Transfers (open) Systems PM/PM10/PM2.5 BACT Analysis

This section presents the PM/PM10/PM2.5 BACT analysis for the open HBI transfer systems designed to occur outside of building enclosures. The open HBI transfer points include the following:

(a) Transfer of HBI from conveyor to stacker machine. (b) Transfer of HBI from stacker machine to HBI stockpile. (c) Transfer of HBI from reclaim bucket wheel to conveyor or reclaim FEL to travelling

hoppers. (d) Transfer of HBI from hoppers to conveyors. (e) HBI loadout to rail and trucks (partial enclosure).

5.15.1 PM/PM10/PM2.5 BACT Baseline There are no state, local or federal regulations applicable to PM/PM10/PM2.5 emissions from the open transfer and handling of HBI. Therefore, there is no “BACT baseline” for this operation.

5.15.2 Step 1 – Identify Available PM/PM10/PM2.5 Control Options HBI transfer systems result in release of small amount particulate matter emissions. The potential control options for controlling emissions from the open HBI transfer systems are identified below:

(a) Fabric filter (baghouse)

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(b) Electrostatic precipitator (ESP) (c) Venturi scrubber (d) Cyclone (e) Water or chemical suppressants (f) Enclosures (g) Windshield

5.15.3 Step 2 – Eliminate Technically Infeasible PM/PM10/PM2.5 Controls The open transfer of HBI by definition results in particulate matter emissions that are fugitive. OAC 3745-31-01(UU) defines fugitive emissions as “…those emissions that cannot reasonably pass through a stack, chimney.” Since these operations are designed to occur in open areas, it is unreasonable to capture emissions from these open transfers. Therefore, add-on control technologies (baghouse, ESP, scrubber, cyclone) are not technically feasible for these operations. In addition, due to specific nature of the operations, i.e. mobile equipment such as stacker/reclaim machine, FEL etc., use of hoods or capture systems are also not technically feasible.

5.15.4 Step 3 – Rank PM/PM10/PM2.5 Control Options The particulate matter control strategies selected for the proposed open transfer of HBI that are considered technically feasible and associated control efficiencies are:

• Water or chemical suppressants - 95% • Enclosure with doors for truck loadout –95% • Enclosure with strip curtains for rail loadout with water sprays – 95%

5.15.5 Step 4 – Evaluate Feasible PM/PM10/PM2.5 Control Options As shown in Appendix B, the open HBI transfer points will either use water or chemical suppressants to control fugitive PM/PM10/PM2.5 emissions. In addition, transfer of HBI from the loadout bins to the rail and the trucks will occur inside the loadout enclosures. Use of these controls are the top control technologies and will not have any material adverse energy, environmental or economic impacts. Therefore, it is appropriate that use of wet suppression or enclosures form the basis for establishing the fugitive PM/PM10/PM2.5 BACT requirements for the proposed open HBI transfer equipment.

5.15.6 Step 5 – Establish PM/PM10/PM2.5 BACT Equipment design or work practice requirements are acceptable under the definition of BACT when technological or economic limitations on the application of measurement methodology would make the imposition of an emissions standard infeasible. That criterion is met with respect to particulate matter emissions from the open HBI transfer systems. The use of water or chemical suppressants or enclosures represents the top ranked control option for the open HBI transfer systems and is deemed as BACT for fugitive PM/PM10/PM2.5 emissions from these operations.

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5.16 Front End Loaders Movement on Unpaved Surfaces PM/PM10/PM2.5 BACT Analysis

This section presents the required PM/PM10/PM2.5 BACT analysis for the fugitive particulate matter emissions from the FELs travel for various materials reclaim activities. The FELs travel on unpaved surfaces in various material stockpile areas. The FEL reclaim activities on unpaved surfaces include the following:

(a) Lumps reclaim and transfer to truck. (b) Fines reclaim and transfer to truck. (c) REMET reclaim and transfer to hopper. (d) HBI reclaim and transfer to hopper. (e) Feed recovery reclaim to hopper. (f) Oversize product reclaim to hopper.

We conservatively used U.S. EPA’s AP-42 emission factors for vehicle movement on unpaved roads in 13.2.2, for estimating particulate matter emissions from the FELs movement in the storage areas.

5.16.1 PM/PM10/PM2.5 BACT Baseline There are no state, local or federal regulations applicable to PM/PM10/PM2.5 emissions from FEL movement on unpaved surfaces at the HBI Facility. Therefore, there is no “BACT baseline” for this operation.

5.16.2 Step 1 – Identify Available PM/PM10/PM2.5 Control Options A summary of the precedents from U.S. EPA’s RBLC database and other known permit precedents for the vehicle transport on unpaved surfaces is presented in Table 5-7.

Table 5-7. Summary of PM/PM10/PM2.5 BACT Precedence for Unpaved Roads RBLC ID/ State Facility Name Permit Date Process Description Control Emission Limit

OK-0173 CMC Steel Oklahoma 1/19/2016 Unpaved roads

Watering and chemical

stabilization (from permit)

NA

MD-0046 Keys Energy Center 10/31/2014 Unpaved roads Watering NA

MD-0042 Wildcat Point Generating Facility 4/8/2014 Unpaved roads Reasonable precautions NA

OH-0344 V&M Star 1/27/2011 Unpaved roads

Watering or chemical

stabilization or suppressants at

sufficient frequencies

PM - 38.3 tons/year PM10 – 7.7

tons/year

LA-0239 Consolidated Environmental Mgmt. 05/24/2010 Unpaved roads Watering or

chemical suppression

PM - 18.69 lb/hour

The proposed FEL’s movement for reclaim and transfer of various materials result in release of a small amount of fugitive particulate matter emissions from lifting of silt by the vehicle

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tires/tracks. The potential control options for controlling emissions from these operations are identified below:

(a) Paving of unpaved roads (b) Watering and/or chemical stabilization

5.16.3 Step 2 – Eliminate Technically Infeasible PM/PM10/PM2.5 Controls Paving of the surfaces within the stockpiles area is not technically feasible because use of heavy FELs for the various reclaim activities will damage the paved surfaces. Watering and/or chemical stabilization is technically feasible for controlling PM/PM10/PM2.5 emissions from the movement of FELs in unpaved areas.

5.16.4 Step 3 – Rank PM/PM10/PM2.5 Control Options No ranking is necessary as only the watering and/or chemical stabilization is technically feasible option for these operations.

5.16.5 Step 4 – Evaluate Feasible PM/PM10/PM2.5 Control Options As shown in Appendix B, the FELs movement on unpaved surfaces will use watering and/or chemical stabilization to control particulate matter emissions (considering weather). Use of the top control technology will not have any material adverse energy, environmental or economic impacts. Therefore, it is appropriate that use of watering and/or chemical stabilization form the basis for establishing the PM/PM10/PM2.5 BACT for the fugitive emissions from the FELs.

5.16.6 Step 5 – Establish PM/PM10/PM2.5 BACT Equipment design or work practice requirements are acceptable under the definition of BACT when technological or economic limitations on the application of measurement methodology would make the imposition of an emissions standard infeasible. That criterion is met with respect to fugitive particulate matter emissions from the FELs material reclaim and transfer operations. The use of watering and/or chemical stabilization represents the top ranked control option for these operations constitute BACT for fugitive PM/PM10/PM2.5.

5.17 Trucks Movement on Paved Roads PM/PM10/PM2.5 BACT Analysis

This section presents the required PM/PM10/PM2.5 BACT analysis for the fugitive particulate matter emissions from the trucks travel for various materials transport activities. The trucks will travel on paved roads to various material stockpile areas. The truck transport activities on paved roads include the following:

(a) Lumps transport. (b) Fines transport. (c) Cement coating transport. (d) HBI transport. (e) Wastewater treatment sludge transport

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We used U.S. EPA’s AP-42 emission factors for vehicle movement on paved roads in 13.2.1, for estimating particulate matter emissions from the truck travel on the paved roads.

5.17.1 PM/PM10/PM2.5 BACT Baseline There are no state, local or federal regulations applicable to PM/PM10/PM2.5 emissions from truck travel on paved roads at the HBI operations. Therefore, there is no “BACT baseline” for this operation.

5.17.2 Step 1 – Identify Available PM/PM10/PM2.5 Control Options A summary of the precedents from U.S. EPA’s RBLC database and other known permit precedents for the trucks’ use on paved roads is presented in Table 5-8. The proposed trucks’ travel for transport of various materials result in release of small amount of fugitive particulate matter emissions from resuspension of loose material on the road surfaces. The potential control option for controlling emissions from these operations is use of water flushing and sweeping (considering weather).

5.17.3 Step 2 – Eliminate Technically Infeasible PM/PM10/PM2.5 Controls Water flushing and sweeping is technically feasible for controlling fugitive PM/PM10/PM2.5 emissions from the truck travel activities on paved roads.

Table 5-8. Summary of PM/PM10/PM2.5 BACT Precedence for Paved Roads RBLC ID/ State Facility Name Permit Date Process Description Control Emission Limit

IN-0263 Midwest Fertilizer Company 3/23/2017 Paved roads

Wet suppression and prompt

cleanup

NA

MD-0046 Keys Energy Center 10/31/2014 Paved roads Sweeping NA

MD-0042 Wildcat Point Generating Facility 4/8/2014 Paved roads Reasonable precautions NA

IN-0179 Ohio Valley Resources LLC 9/25/2013 Paved roads Sweeping and

wet suppression

90% control efficiency

IN-0166 Indiana Gasification 6/27/2012 Paved roads Sweeping and

wet suppression

90% control efficiency

OH-345 DP&L JM Stuart Generating Station 8/16/2011 Paved roads Watering and reduced speed 110.96 tons/year

OH-0344 V&M Star 1/27/2011 Paved roads

Watering or chemical

stabilization or suppressants at

sufficient frequencies

PM - 38.3 tons/year PM10 – 7.7

tons/year

5.17.4 Step 3 – Rank PM/PM10/PM2.5 Control Options No ranking is necessary as only the water flushing and sweeping is technically feasible option for these operations.

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5.17.5 Step 4 – Evaluate Feasible PM/PM10/PM2.5 Control Options As shown in Appendix B, the truck travel on paved roads will use water flushing and sweeping to control fugitive particulate matter emissions. Use of the top control technology will not have any material adverse energy, environmental or economic impacts. Therefore, it is appropriate that use of water flushing and sweeping form the basis for establishing the fugitive PM/PM10/PM2.5 BACT for the proposed truck travel activities.

5.17.6 Step 5 – Establish PM/PM10/PM2.5 BACT Equipment design or work practice requirements are acceptable under the definition of BACT when technological or economic limitations on the application of measurement methodology would make the imposition of an emissions standard infeasible. That criterion is met with respect to particulate matter emissions from the truck material transport operations. Use of water flushing and sweeping represents the top ranked control option for these operations constitute BACT for fugitive PM/PM10/PM2.5.

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6. Ambient Air Quality Impacts Analysis This section presents a summary of the updated PSD ambient air quality impacts analysis. The modeling report, including detailed information regarding model selection, receptor location, and modeling procedures, are included as Appendix D. Even though the proposed change to the Project resulted in revisions to a subset of criteria pollutant/emissions unit combinations, the modeling analysis addresses all units and pollutants that were addressed in the prior PTI application. The Project results in ‘significant’ emissions for PM, PM10, PM2.5, NOx, CO, and GHGs. Based on historical precedence, and U.S. EPA’s guidance, impacts analysis is not required for PM and GHGs.21 22 This section addresses impacts of other criteria pollutants for which the area is attainment or unclassifiable.

6.1 Emissions Rates for Modeling Purposes The emissions rates used for modeling purposes represent the worst case short term and long term rates for each of the proposed units. These rates are presented in Appendix B and Appendix D of this application. As previously noted, consistent with OEPA guidance, emissions from the proposed intermittent operations (emergency engines and flaring during process upset/startup/shutdown) are not included for demonstrating compliance with short term national ambient air quality standards (NAAQS).

6.2 Summary of Class II Modeled Impacts This section presents the modeling results for the HBI Facility for Class II areas.

6.2.1 Class II Significant Impacts Analysis Emissions from the proposed project are modeled in accordance with the modeling protocol submitted in August 2017 and the follow-up discussions and submittals. The resulting ambient impacts are compared with the Class II significant impact levels (“SILs”) codified at OAC 3745-31-23 and issued by the U.S. EPA in 40 CFR § 51.165(b)(2) or by guidance. In accordance with the OEPA and U.S. EPA’s procedures, if the maximum ambient impacts from the project are below the particular SIL, the project is presumed to neither cause nor contribute to a violation of the NAAQS or PSD increment for that pollutant. Pollutants with impacts that exceed the SIL, will be included in both the NAAQS and increment analyses. Table 6-1 presents the Class II significant impacts analyses for the proposed Project.

21 75 Fed. Reg. 31514, June 3, 2010, page 31520. 22 In a March 2011 permitting guidance issued by the U.S.EPA, it observed that “[s]ince there are no NAAQS or PSD increments for GHGs, the requirements .. to demonstrate that a source does not cause or contribute to a violation of the NAAQS is not applicable to GHGs. Thus, we do not recommend that PSD applicants be required to model or conduct ambient monitoring for CO2 or GHGs.” [footnotes omitted] PSD and Title V Permitting Guidance for Greenhouse Gases, EPA-457/B-11-001, March 2011, at pages 47-48.

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Table 6-1. Class II Significant Impact Analysis Result Pollutant Average Model Conc.

(µg/m3) SIL

(µg/m3)

NO2 1-HR 14.5 7.5 ANNUAL 1.25 1.0

CO 1-HR 3,010 2000 8-HR 1,744 500

PM10 24-HR 27.2 5.0 ANNUAL 2.53 1.0

PM2.5 24-HR 7.03 1.2 ANNUAL 0.97 0.3

For the proposed Project, predicted impacts exceed the applicable SIL for NO2, CO, PM10 and PM2.5 NAAQS for all averaging periods. Therefore, these criteria pollutants were further analyzed for cumulative modeling that includes nearby sources. For all other pollutant-averaging time combinations, the project impacts are below the SIL.

6.2.2 Summary of NAAQS Analysis The NAAQS analyses results are presented below. The modeling analyses were performed using AERMOD. Table 6-2 presents the NAAQS analyses for the proposed Project that exceed the SIL.

Table 6-2. NAAQS Analysis Result Pollutant Average Model Conc.

(µg/m3) Background

(µg/m3) Total

(µg/m3) NAAQS (µg/m3)

Notes

NO2 1-HR 168.5 Paired within model 168.5 188

NOx Annual 7.52 17.68 25.2 100

PM2.5

24-HR 9.38 21.5 30.9 35

Total includes 0.07 µg/m3 secondary contribution

ANNUAL 2.08 8.22 10.3 12

Total includes 0.002 µg/m3 secondary contribution

PM10 24-HR 45.2 35 80.2 150

CO 1-HR 2,845.0 2,743 5,588.2 40,000 8-HR 1,429.35 1,863 3,292.4 10,000

The Project impacts for all criteria pollutants are below the applicable NAAQS. Detailed results are presented in Appendix D.

6.2.3 Class II PSD Increment Analysis PM10, PM2.5, and NOx increment analyses were conducted for the proposed Project. Table 6-3 presents the increment analyses for the proposed Project. The increment analysis addressed the requirement both for overall impacts to be below the applicable increment and project impacts to be below the 83% of increment for the projects located at brownfield sites

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Table 6-3. Increment Analysis Result

Pollut-ant

Average Case Model Conc. (µg/m3)

Standard (µg/m3)

Notes

PM2.5

24-HR All Sources 7.16 (includes 0.07

secondary contribution) 9.0 Cumulative impacts

HBI Only 7.02 (includes 0.07 secondary contribution) 7.5 Project <83% of Increment

Annual All Sources 1.18 (includes 0.002

secondary contribution) 4.0 Cumulative impacts

HBI Only 1.07 (includes 0.002 secondary contribution) 2.0 Project <50% of Increment.*

PM10 24-HR All Sources 26.3 30.0 Cumulative impacts

HBI Only 23.5 24.9 Project <83% of Increment

Annual All Sources 4.20 17.0 Cumulative impacts HBI Only 2.51 8.5 Project <50% of Increment.*

NOx Annual All Sources 7.52 25.0 Cumulative impacts HBI Only 1.25 12.5 Project <50% of Increment.*

* For the cases where project impacts are below the 50% of increment, per OEPA Engineering Guide 69 additional comparison with 83% of the increment is not necessary.

The increment analysis shows that modeled concentration for the Project are below the applicable Class II increment thresholds.

6.2.4 Visibility Analysis in Class II Areas A visibility analysis for the proposed Project impacts on the Class II areas is conducted using the VISCREEN model. Results of this analysis are presented in Appendix D. This analysis indicates that the Project impacts will not exceed the visibility screening criteria. The Project therefore will not adversely affect visibility at the Cuyahoga Valley National Park, which is over 100 miles (>160 km) from the HBI facility.

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7. Site Air Quality Analysis Per OAC 3745-31-14, an applicant for a PSD permit is required to collect pre-construction ambient air quality data for each pollutant for which the project PTE is significant. OAC 3745-31-13(H) provides exemptions from pre-application monitoring requirements for the Project. Based on the EPA guidance, if sufficient data exists to provide representative regional background concentrations, agency may waive the preconstruction monitoring requirement.23 IU previously provided this demonstration in the modeling protocol submitted on August 4, 2017 and requested a waiver from the preconstruction monitoring requirements for the proposed Project per OAC 3745-31-13(H)(4). Available data from the existing monitors in the area is provided in the air dispersion modeling report in Appendix D. OEPA granted the requested waiver per the original PTI P0123395.

23 “Circuit Court Decision on PM2.5 Significant Impact Levels and Significant Monitoring Concentration,” USEPA, March 4, 2013, at http://epa.gov/nsr/documents/20130304qa.pdf.

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8. Additional Impacts Analyses An additional impacts analysis was performed consistent with the requirements of OAC 3745-31-17 (Attainment Provisions – Additional Impacts Analysis) to determine potential air emissions impacts on soils, vegetation, visibility, and growth as part of the original PTI application. The revised Project will emit PM, PM10, PM2.5, NOx, and CO in excess of the PSD significant emission rates and are therefore considered in the analysis. Per the U.S. EPA’s guidance the additional impacts analyses requirements do not apply to the emissions of GHGs from the project. 24 25

8.1 Effects on Soil The pollutants included in this analysis of the potential impairment to soils are PM10, PM2.5 CO, and NOx. The results of the soils impact analysis show that no significant impairment will occur as a result of the construction or operation of the proposed Project. Specific findings are documented in the following subsections.

8.1.1 Soil Survey Over 88,000 acres (138 square miles) surrounding the site of the proposed Project were evaluated for the soils analysis using the U.S. Department of Agriculture Natural Resource Conservation Service Web Soil Survey application. The area evaluated encompasses portions of Lucas, Ottawa, and Wood Counties in Ohio and Monroe County in Michigan.26 As presented in Table 8-1, the primary soil type in this area is some variety of silty clay loam at over 28 percent of the total acreage in the study. Other types of soil in significant quantities around the facility include Udorthents loam, Colwood loam and combinations of urban land and Dixboro, Bixler, Del-Ray, Sisson, and Colwood loam. The pH of these soils ranged from 6.5 to 7.3.

The U.S. Department of Agriculture (USDA) considers approximately 33 percent of this land to be prime farmland if irrigated. No portion of the study area was identified as farmland of unique importance. Further, the USDA soil survey rated all of the soil types listed in Table 8-1 as having somewhat or very limited use for recreational activities such as camping, paths and trails, picnic areas, and playgrounds, with the exception of the following for which no rating was provided: udorthents, urban land, Lenawee-urban land complex, Sisson-urban land complex, and Ottokee-urban land complex. Less than 5 percent of the total study area is identified as having unlimited recreational value, specifically for use as golf fairways.

24 75 Fed. Reg. 31514, June 3, 2010, page 31520. 25 In a March 2011 permitting guidance, the U.S.EPA observed that “…it is not necessary for applicants or permitting authorities to assess impacts from GHGs in the context of the additional impacts analysis or Class I area provisions of the PSD regulations… EPA believes that the most practical way to address the considerations reflected in the Class I area and additional impacts analysis is to focus on reducing GHG emissions to the maximum extent.” PSD and Title V Permitting Guidance for Greenhouse Gases, EPA-457/B-11-001, March 2011, at pages 47-48. 26 U.S. Department of Agriculture, Natural Resource Conservation Service, Custom Soil Resource Report for Lucas County, OH, Monroe County, MI, Ottawa County, OH, and Wood County, OH. July 10, 2017.

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Table 8-1. Major Soil Types in Study Area Map Unit Name Acres Percent of Total pH

Latty silty clay, till substratum, 0 to 1 percent slopes 18,084.9 23.4 7.2 Udorthents, loamy 7,982.3 10.3 - Urban land 5,384.8 7.0 - Dixboro-Urban land complex, 0 to 2 percent slopes 4,814.2 6.2 6.7 Bixler-Urban land complex, 0 to 3 percent slopes 3,310 4.3 6.5 Del-Ray-Urban land complex, 0 to 3 percent slopes 3,043 3.9 7.3 Toledo silty clay, 0 to 1 percent slopes 2,987.6 3.9 6.9 Fulton silty clay loam, 0 to 2 percent slopes 2,546.8 3.3 6.7 Lenawee silty clay loam, 0 to 1 percent slopes 1849.9 2.4 7.2 Sisson-Urban land complex, 2 to 12 percent slopes 1,325.6 1.7 7 Colwood-Urban land complex 1,297.3 1.4 7.3 Colwood loam 1,111.1 1.4 7.3

8.1.2 Pollutant Impacts on Soils Current literature contains little information on impairment or other direct effects on soils due to air pollution, and we did not identify as part of this analysis any studies in which potential pollutant effects on the soils specific to the project area were evaluated. This is consistent with U.S. EPA’s findings on this topic:

In contrast to the amount of published information on the effects of atmospheric pollutants on plants and animals, very little has been reported on their effects on soils. Research on trace elements in soils, often the same elements as atmospheric pollutants, has been directed to notable deficiencies or excesses that limit agricultural crop production. When the amount of an atmospheric pollutant entering a soil system is sufficiently small, the natural ecosystem can adapt to these small changes in much the same way as the ecosystem adapts to the natural weathering processes that occur in all soils. Cultural practices (e.g., liming, fertilization, use of insecticides and herbicides) add elements and modify a soil system more than a small amount of deposited atmospheric pollutant can The secondary effects of the pollutant appear to impact the soil system more adversely than the addition of the pollutant itself to the soil. For instance, damaging or killing vegetative cover could lead to increased solar radiation, increased soil temperatures, and moisture stress. Increased runoff and erosion add to the problem. The indirect action of the pollutant, through changes to the stability of the system, thus may be more significant than the direct effects on soil invertebrates and soil microorganisms. However the lack of long-term historical data on both the type and amount of atmospheric pollutants as well as the lack of baseline data on soils has made difficult the task of determining the effect of pollutants on soils by monitoring changes associated with exposure to pollutants. A limited number of studies have been carried out on trace element contamination in soils. Plant and animal communities appear to be affected before noticeable accumulations occur in the soils. Thus, the approach used here in which the soil acts as an intermediary in the

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transfer of deposited trace elements to plants appears reasonable as a first attempt at identifying the air quality related values associated with soils.27

Because deposition of NOx and other nitrogen compounds into soils in the survey area could occur as a result of emissions from the construction and operation of the proposed Project, it is reasonable to consider whether some marginal acidification of the soils might occur as a result of this project. As presented in Table 8-1, the majority of the major soil types in the survey area are alkaline (i.e., pH greater than 7.0), meaning that some degree of acidification can be readily tolerated and may in fact be desirable. Based on these facts, we have concluded that the proposed facility will not have an adverse impact on soils.

8.2 Effects on Vegetation This analysis of impacts to vegetation covers the entirety of the Lucas, Ottawa, and Wood Counties in Ohio and Monroe County in Michigan. This study area exceeds the scope suggested by U.S. EPA guidance, which is limited to the area within the impact area of the proposed facility (10km).28

8.2.1 Vegetation Survey The natural vegetation located in these counties is primarily deciduous forest consisting of oak, hickory, ash, and maple varieties.2930 According to a 2010 Ohio forest resource assessment conducted by the Ohio Department of Natural Resources Division of Forestry31, approximately 12% of Lucas County is forested. The forested areas of Ottawa and Wood Counties is approximately 8%. The forested acreage in Monroe County, Michigan is approximately 10% of the total county area.32

Information provided in the 2012 USDA Census reports for Michigan and Ohio was used to identify commercial vegetation in the study area. 3334 The major crops are presented in Table 8-2. As shown, approximately 50 percent of the land included in the study area is used for harvested crops. Of this total, 94 percent is used for soybeans, corn for grain, and wheat for grain. Other crops each harvested from less than 1 percent of the harvested area include forage, oats for grain, and vegetables. Specific locations for the farms for these harvested crops is not provided in the Census reports. Visual

27 Smith, A.E., and J.B. Levenson. A Screening Procedure for the Impacts of Air Pollution Sources on Plants, Soils, and Animals (EPA-450/2-81-078). U.S. EPA, Office of Air Quality Planning and Standards. Research Triangle Park, NC. December 1980. Pp. 17-19. 28 See, e.g., Prevention of Significant Deterioration Workshop Manual (EPA-450/2-80-081), Oct. 1980, at page I-D-6, expressly limiting the soils and vegetation impairment analysis to the “impact area”. See also the same document at page I-C-12, defining the impact area as a “circular area whose radius is equal to the greatest distance from the source to which approved dispersion modeling shows the proposed emissions will have a significant impact.” 29 Resource Bulletin NRS-36 Ohio Forests 2009 30 Forest & Forestry Profile for Michigan Senate District 17, Bill Cook, MSU Extension, January 2006 31 Ohio’s Statewide Forest Resource Assessment, Ohio Department of Natural Resources, Division of Forestry, June 2010. 32 Forest & Forestry Profile for Michigan Senate District 17, Bill Cook, MSU Extension, January 2006 33 2012 Census of Agriculture, Michigan State and County Data, Volume 1, Issued May 2014. 34 2012 Census of Agriculture, Ohio State and County Data, Volume 1, Issued May 2014..

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inspection of aerial photographs of the area suggests the majority of the harvested areas are located beyond 10km radius of the HBI Facility.

8.2.2 Identification of Pollutants of Concern As discussed below, there are substantial scientific data characterizing the effects of air pollution on certain crops (e.g., common wheat), whereas there are limited data available for other crops. Air pollutants can affect crops through two principal means:

• Direct phytotoxic effects from air concentrations of pollutants; and, • Indirect phytotoxic effects due to deposition of pollutants in soils in which the crops are

growing.

Table 8-2. Land Use for Commercially Significant Vegetation in Study Area1,2

Vegetation Lucas Ottawa Wood Monroe Total

Corn (grain) 21,940 25,964 87,393 76,225 211,522

Forage 468 3,885 4,494 3,827 12,674

Oats (grain) - 396 373 208 977

Soybeans 30,690 60,815 122,804 82,227 296,536

Vegetables 1,286 1,699 1,285 8,459 12,729

Wheat (grain) 3,663 3,782 21,739 16,897 46,081

Total Harvested Area 58,387 97,054 242,238 189,032 586,711

Total Land Area of Study 217,894 163,168 395,085 435,200 1,211,347 12012 Census of Agriculture, Michigan State and County Data, Volume 1, Issued May 2014. Data presented as harvested acres. Crops with greater than 200 acres harvested considered for this analysis. 22012 Census of Agriculture, Ohio State and County Data, Volume 1, Issued May 2014. Data presented as harvested acres. Crops with greater than 200 acres harvested considered for this analysis.

8.2.2.1 Direct Phytotoxic Effects Of the gaseous air pollutants covered by this analysis, only NOx (i.e., NO and NO2) is known to be toxic to some plants at moderate to high concentrations in the ambient air. Carbon monoxide is not considered phytotoxic, thus it was not considered further by this analysis.35 Studies linking gaseous 35 Air Quality Criteria for Carbon Monoxide. U.S. Department of Health, Education, and Welfare, Public Health Service, National Air Pollution Control Administration. Washington, DC. March 1970. PP. 7-1 through 7-3.

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species of nitrogen to plant foliar damage have been conducted well above concentration levels occurring in the United States. Thus, there is little evidence to show that current U.S. concentrations of gaseous phase nitrogen cause phytotoxic effects.36 In the 2008 review of the secondary NO2 NAAQS, EPA concluded that agricultural ecosystems are not sensitive to nitrogen concentrations found in the U.S.37

8.2.2.2 Indirect Effects The particulate matter emissions from the proposed Project may contain trace quantities of chromium, copper, fluoride, lead, manganese, nickel, and zinc which have been found to adversely affect plants.38 However, because the Project will emit these contaminants at such low levels, it is unlikely that these emissions will significantly impact vegetation adjacent to the facility.

8.2.3 Determination of Effects Concentrations

8.2.3.1 Direct Phytotoxic Effects As is customary for this type of analysis, the assessment relied heavily on the screening criteria in the U.S. EPA report, A Screening Procedure for the Impacts of Air Pollution Sources on Plants, Soils, and Animals.39 This document establishes the air pollutant concentrations that are generally viewed by U.S. EPA to be protective of soils and vegetation having significant commercial or recreational value, including agricultural crops, based on a broad review of pertinent scientific literature. We also relied on the secondary National Ambient Air Quality Standards (NAAQS),40 which are established by U.S. EPA at levels that are protective of the public welfare, including agriculture.

8.2.3.2 Indirect Deposition Effects Two general approaches have been used in establishing deposition rate limits and soil concentration limits: a) preventing accumulation of pollutants in soils; and b) maximizing the capacity of soils to assimilate, attenuate, and detoxify pollutants. The first approach is based on the premise that soil can be used without any undue restriction if it is maintained free of contamination; if pollutants are artificially introduced and are allowed to accumulate in the soil, then, over the long term, the potential uses of the soil may become limited. The second approach is based on the premise that soils have a capacity to detoxify pollutants. This approach has been applied by the U.S. EPA and by the World Health Organization.41

36 “Executive Summary Integrated Science Assessment Oxides of Nitrogen and Sulfur Ecological Criteria.” EPA/600/R-08/082F, Dec. 2008. 37 Ibid 38Smith, A.E., and J.B. Levenson. A Screening Procedure for the Impacts of Air Pollution Sources on Plants, Soils, and Animals (EPA-450/2-81-078). U.S. EPA, Office of Air Quality Planning and Standards. Research Triangle Park, NC. December 1980. P. 17. 39 Ibid 40 See, 40 CFR part 50. 41 A.C. Chang, et al. Developing Human Health-related Chemical Guidelines for Reclaimed Water and Sewage Sludge Applications in Agriculture. World Health Organization. Copenhagen, Denmark. May 2002. pp. 19-41.

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8.2.4 Results This section presents the results of dispersion modeling (and deposition calculations, where applicable) for each air pollutant, and assesses these results with respect to effects levels.

PM10/PM2.5 Effects: As shown in section 6, the Project particulate matter impacts for PM10 and PM2.5 are below the secondary standards both for 24-hour and annual NAAQS. Therefore, particulate matter emissions from the Project will not adversely affect the vegetation in the area.

NOx Effects: NOX includes both nitric oxide (NO) and nitrogen dioxide (NO2), and much of the scientific literature treats these two gases separately. Based on the results of the air quality impacts analysis, the maximum predicted ambient NOX concentrations due to emissions from the proposed Project are 8.89 μg/m3 (1-hour average) and 0.86 μg/m3 (annual average). These values represent total NOX, including both NO and NO2. These impacts are several orders of magnitude below the secondary NAAQS of 100 μg/ m3 (annual average)42 and the minimum U.S. EPA screening values of 3,760 μg/ m3 (4-hr average) and 94 μg/ m3 (annual average).43 Both the secondary NAAQS and the screening value are expressed in terms of NO2; there are no NAAQS or screening values for NO.44 The agricultural crops for which the minimum U.S. EPA screening value is listed as being protective include all of the primary crops identified above (i.e., beans, corn, and wheat).45 The literature was reviewed to ascertain whether there exists, in the scientific literature, any basis for concluding that: a) the secondary NAAQS and the minimum U.S. EPA screening value are not protective of any of the crops identified herein; or b) the Project’s NOX emissions will have an unacceptable, adverse impact on agricultural crops in the study area. A summary of our findings follows. In April 2012, U.S. EPA issued a final rule retaining and affirming the secondary NO2 NAAQS of 100 μg/ m3 (annual average).46 This action reflected both the U.S. EPA Administrator’s finding that this standard is “adequate to protect against direct phytotoxic effects on vegetation”47 and her judgment that an alternative standard to protect against deposition-related effects is not supported by currently available data.48 The data relied upon by U.S. EPA with respect to direct phytotoxic effects are summarized in the Integrated Science Assessment,49 including the following observation:

42 40 CFR § 50.11(c). 43 Smith, A.E., and J.B. Levenson. A Screening Procedure for the Impacts of Air Pollution Sources on Plants, Soils, and Animals (EPA-450/2-81-078). U.S. EPA, Office of Air Quality Planning and Standards. Research Triangle Park, NC. December 1980. p. 11. 44 Ibid. 45 Ibid at p. 68. 46 See, generally, 77 Fed. Reg. 20218. April 3, 2012. 47 Ibid at p. 20241. 48 Ibid at pp. 20262-63. 49 Integrated Science Assessment for Oxides of Nitrogen and Sulfur – Ecological Criteria (EPA-600/R-08-082F). U.S. EPA, Office of Research and Development. Research Triangle Park, NC. December 2008.

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An analysis of over 50 peer-reviewed reports on the effects of NO2 on foliar injury indicated that plants are relatively resistant to NO2. With few exceptions, visible injury was not reported at concentrations below 377 μg/ m3, and these occurred when the cumulative duration of exposures extended to 100 hours or longer.

In 2000, the WHO instituted a NOX guideline concentration value of 30 μg/m3 on an annual average (including both NO and NO2, expressed as NO2). The WHO declined to institute a short-term value, saying “[t]here are insufficient data to provide these levels with confidence at present,” but indicated that current evidence would suggest a guideline NOX concentration value of about 75 μg/m3 on a daily average. The guideline concentration value is intended to be protective of all classes of vegetation under all environmental conditions.50 CO Effects: As shown in section 6, the Project CO impacts are below the applicable NAAQS. Therefore, CO emissions from the Project will not adversely affect the vegetation in the area. In summary, nothing in the scientific literature reviewed indicates that the secondary NAAQS and the minimum annual U.S. EPA screening value are not protective of any of the crops identified herein. The maximum predicted NOX concentration is well below the secondary NAAQS, the minimum U.S. EPA screening value, guideline concentration values established by foreign governmental agencies, and concentrations that are identified in the literature as being harmful to commercially significant vegetation in the study area.

8.3 Soil and Vegetation Analysis Conclusion Based on the effects analysis described herein, we conclude that emissions from the proposed Project are not expected to result in adverse effects to soils, crops, or plant species of concern, within the vicinity of the project site. For each pollutant of concern, the predicted ambient concentration or the predicted deposition rate is well below the secondary NAAQS and the minimum screening values established by U.S. EPA. Nothing in the scientific literature identified during this review indicates that the secondary NAAQS and minimum U.S. EPA screening values are not protective of any identified crops, and the predicted ambient concentration and deposition rate are less than the screening values established by other governmental authorities.

8.4 Visibility The Class II visibility impacts are discussed in subsection 6.2.4 and Appendix D of the application.

8.5 Growth Impact Analysis The purpose of the growth analysis is to quantify the associated industrial, commercial, and residential growth that will occur in the area due to the Project. The associated growth is the growth

50 Air Quality Guidelines for Europe, 2nd Ed. World Health Organization, Regional Office for Europe. Copenhagen, Denmark. 2000. pp. 230-233.

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that occurs as a result of the construction or modification of the source, but which is not part of the source. The emissions that result from this growth are then estimated and the effects of these emissions on the surrounding environment are determined. The growth analysis addresses only permanent economic growth attributable to the proposed Project. Short-term or temporary impacts, such as construction, are not considered permanent growth and therefore are not addressed as an additional impact. Given the large local population, the construction associated with the Project will not have a significant impact to the local population. Construction of the project is expected to result in 130 new, permanent positions at the site, and approximately 1,200 temporary construction positions over two years. It is anticipated that the construction workforce will be drawn, largely from the surrounding communities. Therefore, the effect on air quality from the incremental growth will be insignificant.

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Appendix A – PTI Application Forms

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PTI/PTIO Application A0064540IronUnits LLC - Toledo HBI

0448011992September 12, 2019

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IronUnits LLC - Toledo HBI - 0448011992 Page 1 PTI/PTIO Application - A0064540

Division of Air Pollution Control Sep 12 2019, 16:07:09

Application for Permit-to-Install or Permit-to-Install and Operate

Correction for Application

Correction to application number: A0064254

Reason for correction: Change to facility profile for VOC fugitive emissionsunits.

This section should be filled out for each permit to install (PTI) or Permit to Install and Operate (PTIO) application. A PTI isrequired for all air contaminant sources (emissions units) installed or modified after January 1, 1974 that are subject to OACChapter 3745-77. A PTIO is required for all air contaminant sources (emissions units) that are not subject to OAC Chapter3745-77 (Title V). See the application instructions for additional information.

For OEPA use only: x Installation Request Federally enforceable restrictions

Modification General Permit

Renewal Other

Please summarize the reason for this permit application. This text will be in the public notice that will appear in the newspaper

of the county where the facility is located.

Construction of a new hot briquetted iron manufacturing facility. This applicationis for revisions to the PTI P0123395.

Is the purpose of this application to transition from OAC Chapter 3745-77 (Title V) to OAC Chapter 3745-31 (PTIO)?

No

Establish PER Due Date - Select an annual Permit Evaluation Report (PER) due date for this facility (does not apply to

facilities subject to Title V, OAC Chapter 3745-77). If the PER has previously been established and a change is now desired,

a PER Change Request form must be filed instead of selecting a date here.

PER not applicable (Title V) or due date already established Federal Rules Applicability

New Source Performance Standards (NSPS) New Source Performance Standards are listed under 40CFR 60 - Standards of Performance for New StationarySources.

Subject to subpart:

IIII - Stationary CompressionIgnition Internal CombustionEngines

National Emission Standards for Hazardous AirPollutants (NESHAP) National Emissions Standards for Hazardous Air Pollutantsare listed under 40 CFR 61. (These include asbestos,benzene, beryllium, mercury, and vinyl chloride).

Not affected

Maximum Achievable Control Technology (MACT) The Maximum Achievable Control Technology standardsare listed under 40 CFR 63 and OAC rule 3745-31-28.

Subject, but exempt:

ZZZZ - Reciprocating InternalCombustion Engines

Prevention of Significant Deterioration (PSD) These rules are found under OAC rule 3745-31-10 throughOAC rule 3745-31-20.

Subject to Regulation

Greenhouse Gas Pollutant Prevention of SignificantDeterioration (PSD) These rules are listed under 40 CFR Parts 51, 52.

Subject to Regulation

Non-Attainment New Source Review These rules are found under OAC rule 3745-31-21 throughOAC rule 3745-31-27.

Not affected

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IronUnits LLC - Toledo HBI - 0448011992 Page 2 PTI/PTIO Application - A0064540

112 (r) - Risk Management Plan These rules are found under 40 CFR 68.

Not affected

Title IV (Acid Rain Requirements) These rules are found under 40 CFR 72 and 40 CFR 73.

Not affected

Please explain why you checked "Subject, but exempt" in this question for one or more federal rules. Identify each exemption

and whether the entire facility and/or the specific air contaminant sources included in this permit application is exempted.

Attach an additional page if necessary.

Emergency engines that are subject to NSPS IIII are exempt from NESHAP ZZZZ

Express PTI/PTIO - Do you qualify for express PTI or PTIO processing?

No

Air Contaminant Sources in this Application - Identify the air contaminant source(s) for which you are applying below.

Attach additional pages if necessary. Section II of this application and an EAC form should be completed for each air

contaminant source.

Emissions Unit ID Company Equipment ID (company's name forair contaminant source)

Equipment Description (List all equipment thatare a part of this air contaminant source)

B001 P-2

F001 HR-1, HR-2, HR-3, HR-4, HR-5 Watering and sweeping for pavedroads (HR-1), Watering and sweepingfor paved roads (HR-2), Wateringand sweeping for paved roads (HR-3), Watering and sweeping for pavedroads (HR-4), Watering and sweepingfor paved roads (HR-5)

F002 Storage Piles Chemical stabilization for unpavedsurfaces for FEL-4, Chemicalstabilization for unpaved surfacesfor FEL-5, Chemical stabilizationfor unpaved surfaces for FEL-6,Chemical stabilization for unpavedsurfaces for FEL-1, Chemicalstabilization for unpaved surfacesfor FEL-2, Chemical stabilizationfor unpaved surfaces for FEL-3,Oxide lumps conveyor to stockpile(TR-8), Controls for Reclaim Bucketto Conveyor, Stacking control foroxide stockpile (TR-3), Oxide finesfrom conveyor to stockpile (TR-11),HBI stacking control for stockpile(TR-20), Wind erosion control foroxide stockpile (WE-1), Winderosion control for HBI stockpile(WE-4), Wind erosion control forfeed recovery stockpile (WE-6),Wind erosion control for lumpsstockpile (WE-2), Wind erosioncontrol for fines stockpile (WE-3)

P001 TR-28b, P-1 Scrubber for Bottom Seal Gas (P-1),Charge Hopper Scrubber Exhaust (TR-28b)

P002 P-3 Scrubber for Hot Briquette Exhaust(P-3)

P003 P-4 Scrubber for Briquette CoolingSystem Vent (P-4)

P004 P-5

P005 P-7 Drift Eliminator for Cooling Tower(P-7)

P006 P-8

P007 P-9

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P008 P-6

P009 P-10

P901 MTR-5,TR-1,TR-2,TR-5,TR-6,TR-7,TR10,SR1,TR13a,TR-13b,TR14

Baghouse for Fines Transfer Drop(TR-13b), Baghouse for OxideTransfer to Bucket Elevator (TR-13a), Baghouse for Oxide TransferTower II (TR-6), Baghouse for OxideDay Bins Transfers (TR-10),Baghouse for Oxide Transfer TowerIII (TR-7), Baghouse for CoatingStorage/Transfer and Fines Transfer(TR-14), Baghouse for Oxide FeedConveyor Transfer (TR-28a),Baghouse for Hopper to Conveyor,Baghouse for Oxide Day BinsTransfers (TR-10), Controls forReclaim Conveyor to Conveyor,Baghouse for Oxide Transfer Tower I(TR-1), Baghouse for Oxide ScreensTransfers (SR-1)

P902 TR-17,TR-18,TR-19,TR-21b,TR-22,TR-23,TR-24,TR-25,TR-26,TR-27

HBI Transfer Baghouse Exhaust (TR-18), HBI Transfer Scrubber Exhaust(TR-17), HBI Truck Loadout BaghouseExhaust (TR-25), HBI TransferBaghouse Exhaust (TR-23), HBITransfer Baghouse Exhaust (TR-24)

TMP213487 Equip Leaks from Valves andConnectors

The Emissions Unit ID would have been created when a previous air permit was issued. If no previous permitshave been issued for this air contaminant source, leave this field blank. If this air contaminant source waspreviously identified in STARShip applications as a “Z” source (e.g., Z001), please provide that identification anda new ID will be assigned when the PTI/PTIO is issued.

Trade Secret Information - Is any information included in this application being claimed as a trade secret per Ohio Revised

Code (ORC) 3704.08?

No

Permit Application Contact - Person to contact for questions about this application:

Brandon Heaney Cleveland-Cliffs Inc.IronUnits LLC

Name Title

P.O. Box 166870 Oregon, OH 43616

Street Address City/Township, State Zip Code

5679703348 [email protected]

Phone Fax E-mail

Application Attachments

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694090 Appendix CBACTCalculations

Permitapplicationattachments andsupplements

X

694092 Appendix FGAD

Permitapplicationattachments and

X

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IronUnits LLC - Toledo HBI - 0448011992 Page 4 PTI/PTIO Application - A0064540

supplements

695590 Appendix BEmissionsCalculations

Calculations

X

694093 Appendix ENG Heaters(Exempt)

Permitapplicationattachments andsupplements

X

695591 PermitApplication Text

Permitapplicationattachments andsupplements

X

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Section II - Specific Air Contaminant Source Information Facility ID: 0448011992Emissions Unit ID: B001

Company Equipment ID: P-2

One copy of this section should be filled out for each air contaminant source (emissions unit) covered by thisPTI/PTIO application identified in Section I, Question 5. See the application instructions for additional information.

Air Contaminant Source Installation or Modification Schedule - Check all that apply (must be completed regardless of

date of installation or modification):

New installation (for which construction has not yet begun, in accordance with OAC rule 3745-31-33). When will you beginto install the air contaminant source?after installation permit has been issued

SCC Codes - List all Source Classification Code(s) (SCC) that describe the process(es) performed by this air contaminant

source (e.g., 1-02-002-04).

See Facility Profile

Emissions Information - The following table requests information needed to determine the applicable requirements and the

compliance status of this air contaminant source with those requirements. Suggestions for how to estimate emissions may

be found in the instructions to the Emissions Activity Category (EAC) forms required with this application. If you need further

assistance, contact your District Office/Local Air Agency representative.

If total potential emissions of HAPs or any Toxic Air Contaminant (as identified in OAC rule 3745-114-01) are greater

than 1 ton/yr, fill in the table for that (those) pollutant(s). For all other pollutants, if “Emissions before controls (max),

lb/hr” multiplied by 24 hours/day is greater than 10 lbs/day, fill in the table for that pollutant.

Actual emissions are calculated including add-on control equipment. If you have no add-on control equipment,

“Emissions before controls” will be the same as “Actual emissions”.

Actual emissions and Requested Allowable should be based on operating 8760 hr/yr unless you are requesting federally

enforceable operating restrictions to limit emissions. If so, calculate emissions based on requested operating restrictions

and describe in your calculations.

If you use units other than lbs/hr or ton/yr, specify the units used (e.g., gr/dscf, lb/ton charged, lb/MMBtu, tons/12-

months).

Requested Allowable (ton/yr) is often equivalent to Potential to Emit (PTE) as defined in OAC rule 3745-31-01 and OAC

rule 3745-77-01.

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Particulate emissions(PE/PM) (formerlyparticulate matter, PM)

18.71 18.71 81.96 18.71 81.96

PM # 10 microns indiameter (PE/PM10)

18.71 18.71 81.96 18.71 81.96

PM # 2.5 microns indiameter (PE/PM2.5)

18.71 18.71 81.96 18.71 81.96

Sulfur dioxide (SO2) 5.05 5.05 22.12 5.05 22.12

Nitrogen oxides (NOx) 99.75 99.75 436.89 99.75 436.89

Carbon monoxide (CO) 52.35 52.35 229.29 52.35 229.29

Organic compounds (OC) 1.82 1.82 7.97 1.82 7.97

Volatile organiccompounds (VOC)

1.82 1.82 7.97 1.82 7.97

Lead (Pb) 0 0 0 0 0

Total Hazardous AirPollutants (HAPs)

0.62 0.62 2.74 0.62 2.74

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5.

6.

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Highest single HAP 0.6 0.6 2.61 0.6 2.61

Hazardous Air Pollutants (HAPs):

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Hexane, N- 0.6 0.6 2.61 0.6 2.61

Greenhouse Gas Pollutants:

Pollutant Emissionsbefore

controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

CO2e(ton/year)

Methane 0.74 0.74 3.26 0.74 3.26 68.46

Carbon Dioxide 354764 354764 1553868 354764 1553868 1,553,868

Nitrous Oxide 0.07 0.07 0.33 0.07 0.33 102.3

Best Available Technology (BAT) - For each pollutant for which the Requested Allowable in the above table exceeds 10

tons per year, BAT, as defined in OAC 3745-31-01, is required. Describe what has been selected as BAT and the basis for

the selection:

Please see the PTI application that addresses BACT requirements that alsoconstitute BAT. In addition, for SO2, the PTE of the reformer is greater than 10TPY. See section 4 BAT discussion for this pollutant unit combination.

Control Equipment - Does this air contaminant source employ emissions control equipment?

See Facility Profile

Process Flow Diagram - Attach a Process Flow Diagram to this application for this air contaminant source. See the

application instructions for additional information.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694097 Processflowdiagramfor CorePlantUpdated

Processflowdiagram

X

Modeling information: (Note: items in bold in Tables 7-A and/or 7-B, as applicable, are required even if the tables do

not otherwise need to be completed. If applicable, all information is required An air quality modeling analysis is

required for PTIs and PTIOs for new installations or modifications, as defined in OAC rule 3745-31-01, where either the

increase of toxic air contaminants from any air contaminant source or the increase of any other pollutant for all air

contaminant sources combined exceed a threshold listed below. This analysis is to assure that the impact from the

requested project will not exceed Ohio's Acceptable Incremental Impacts for criteria pollutants and/or Maximum Allowable

Ground Level Concentrations (MAGLC) for toxic air contaminants. (See Ohio EPA, DAPC's Engineering Guide #69 for more

information.) Permit requests that would have unacceptable impacts cannot be approved as proposed. See the line-by-line

PTI/PTIO instructions for additional information.

See Facility Profile

Request for Federally Enforceable Limits - As part of this permit application, do you wish to propose voluntary restrictions

to limit emissions in order to avoid specific requirements listed below, (i.e., are you requesting federally enforceable limits to

obtain synthetic minor status)?

No

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9.

10.

IronUnits LLC - Toledo HBI - 0448011992 Page 3 PTI/PTIO Application - A0064540

Continuous Emissions Monitoring - Does this air contaminant source utilize any continuous emissions monitoring (CEM)

equipment for indicating or demonstrating compliance? This does not include continuous parametric monitoring systems.

See Facility Profile

EAC Forms - The appropriate Emissions Activity Category (EAC) form(s) must be completed and attached for each air

contaminant source. At least one complete EAC form must be submitted for each air contaminant source for the application

to be considered complete. Refer to the list attached to the application instructions. Please indicate which EAC form

corresponds to this air contaminant source.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694113 RevisedEAC FormReformer

EAC 3101 Fuelburningoperation

X 11/14/2017

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1.

2.

3.

-

-

-

-

-

IronUnits LLC - Toledo HBI - 0448011992 Page 1 PTI/PTIO Application - A0064540

Section II - Specific Air Contaminant Source Information Facility ID: 0448011992Emissions Unit ID: F001

Company Equipment ID: HR-1, HR-2, HR-3,HR-4, HR-5

One copy of this section should be filled out for each air contaminant source (emissions unit) covered by thisPTI/PTIO application identified in Section I, Question 5. See the application instructions for additional information.

Air Contaminant Source Installation or Modification Schedule - Check all that apply (must be completed regardless of

date of installation or modification):

New installation (for which construction has not yet begun, in accordance with OAC rule 3745-31-33). When will you beginto install the air contaminant source?after installation permit has been issued

SCC Codes - List all Source Classification Code(s) (SCC) that describe the process(es) performed by this air contaminant

source (e.g., 1-02-002-04).

See Facility Profile

Emissions Information - The following table requests information needed to determine the applicable requirements and the

compliance status of this air contaminant source with those requirements. Suggestions for how to estimate emissions may

be found in the instructions to the Emissions Activity Category (EAC) forms required with this application. If you need further

assistance, contact your District Office/Local Air Agency representative.

If total potential emissions of HAPs or any Toxic Air Contaminant (as identified in OAC rule 3745-114-01) are greater

than 1 ton/yr, fill in the table for that (those) pollutant(s). For all other pollutants, if “Emissions before controls (max),

lb/hr” multiplied by 24 hours/day is greater than 10 lbs/day, fill in the table for that pollutant.

Actual emissions are calculated including add-on control equipment. If you have no add-on control equipment,

“Emissions before controls” will be the same as “Actual emissions”.

Actual emissions and Requested Allowable should be based on operating 8760 hr/yr unless you are requesting federally

enforceable operating restrictions to limit emissions. If so, calculate emissions based on requested operating restrictions

and describe in your calculations.

If you use units other than lbs/hr or ton/yr, specify the units used (e.g., gr/dscf, lb/ton charged, lb/MMBtu, tons/12-

months).

Requested Allowable (ton/yr) is often equivalent to Potential to Emit (PTE) as defined in OAC rule 3745-31-01 and OAC

rule 3745-77-01.

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Particulate emissions(PE/PM) (formerlyparticulate matter, PM)

26.75 1.25 4.20 1.25 4.20

PM # 10 microns indiameter (PE/PM10)

5.35 0.25 0.84 0.25 0.84

PM # 2.5 microns indiameter (PE/PM2.5)

1.31 0.1 0.21 0.1 0.21

Sulfur dioxide (SO2) 0 0 0 0 0

Nitrogen oxides (NOx) 0 0 0 0 0

Carbon monoxide (CO) 0 0 0 0 0

Organic compounds (OC) 0 0 0 0 0

Volatile organiccompounds (VOC)

0 0 0 0 0

Lead (Pb) 0 0 0 0 0

Total Hazardous AirPollutants (HAPs)

0 0 0 0 0

Page 78: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

4.

5.

6.

7.

8.

9.

10.

IronUnits LLC - Toledo HBI - 0448011992 Page 2 PTI/PTIO Application - A0064540

Highest single HAP 0 0 0 0 0

Best Available Technology (BAT) - For each pollutant for which the Requested Allowable in the above table exceeds 10

tons per year, BAT, as defined in OAC 3745-31-01, is required. Describe what has been selected as BAT and the basis for

the selection:

Please see the PTI application that addresses BACT requirements that alsoconstitute BAT.

Control Equipment - Does this air contaminant source employ emissions control equipment?

See Facility Profile

Process Flow Diagram - Attach a Process Flow Diagram to this application for this air contaminant source. See the

application instructions for additional information.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694103 PFD forpaved andunpavedroadways

Processflowdiagram

X

Modeling information: (Note: items in bold in Tables 7-A and/or 7-B, as applicable, are required even if the tables do

not otherwise need to be completed. If applicable, all information is required An air quality modeling analysis is

required for PTIs and PTIOs for new installations or modifications, as defined in OAC rule 3745-31-01, where either the

increase of toxic air contaminants from any air contaminant source or the increase of any other pollutant for all air

contaminant sources combined exceed a threshold listed below. This analysis is to assure that the impact from the

requested project will not exceed Ohio's Acceptable Incremental Impacts for criteria pollutants and/or Maximum Allowable

Ground Level Concentrations (MAGLC) for toxic air contaminants. (See Ohio EPA, DAPC's Engineering Guide #69 for more

information.) Permit requests that would have unacceptable impacts cannot be approved as proposed. See the line-by-line

PTI/PTIO instructions for additional information.

See Facility Profile

Request for Federally Enforceable Limits - As part of this permit application, do you wish to propose voluntary restrictions

to limit emissions in order to avoid specific requirements listed below, (i.e., are you requesting federally enforceable limits to

obtain synthetic minor status)?

No

Continuous Emissions Monitoring - Does this air contaminant source utilize any continuous emissions monitoring (CEM)

equipment for indicating or demonstrating compliance? This does not include continuous parametric monitoring systems.

See Facility Profile

EAC Forms - The appropriate Emissions Activity Category (EAC) form(s) must be completed and attached for each air

contaminant source. At least one complete EAC form must be submitted for each air contaminant source for the application

to be considered complete. Refer to the list attached to the application instructions. Please indicate which EAC form

corresponds to this air contaminant source.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694104 EAC formfor TrucksonroadwaysUpdated

EAC 3111RoadwaysandParkingAreas

X

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1.

2.

3.

-

-

-

-

-

IronUnits LLC - Toledo HBI - 0448011992 Page 1 PTI/PTIO Application - A0064540

Section II - Specific Air Contaminant Source Information Facility ID: 0448011992Emissions Unit ID: F002

Company Equipment ID: Storage Piles

One copy of this section should be filled out for each air contaminant source (emissions unit) covered by thisPTI/PTIO application identified in Section I, Question 5. See the application instructions for additional information.

Air Contaminant Source Installation or Modification Schedule - Check all that apply (must be completed regardless of

date of installation or modification):

New installation (for which construction has not yet begun, in accordance with OAC rule 3745-31-33). When will you beginto install the air contaminant source?after installation permit has been issued

SCC Codes - List all Source Classification Code(s) (SCC) that describe the process(es) performed by this air contaminant

source (e.g., 1-02-002-04).

See Facility Profile

Emissions Information - The following table requests information needed to determine the applicable requirements and the

compliance status of this air contaminant source with those requirements. Suggestions for how to estimate emissions may

be found in the instructions to the Emissions Activity Category (EAC) forms required with this application. If you need further

assistance, contact your District Office/Local Air Agency representative.

If total potential emissions of HAPs or any Toxic Air Contaminant (as identified in OAC rule 3745-114-01) are greater

than 1 ton/yr, fill in the table for that (those) pollutant(s). For all other pollutants, if “Emissions before controls (max),

lb/hr” multiplied by 24 hours/day is greater than 10 lbs/day, fill in the table for that pollutant.

Actual emissions are calculated including add-on control equipment. If you have no add-on control equipment,

“Emissions before controls” will be the same as “Actual emissions”.

Actual emissions and Requested Allowable should be based on operating 8760 hr/yr unless you are requesting federally

enforceable operating restrictions to limit emissions. If so, calculate emissions based on requested operating restrictions

and describe in your calculations.

If you use units other than lbs/hr or ton/yr, specify the units used (e.g., gr/dscf, lb/ton charged, lb/MMBtu, tons/12-

months).

Requested Allowable (ton/yr) is often equivalent to Potential to Emit (PTE) as defined in OAC rule 3745-31-01 and OAC

rule 3745-77-01.

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Particulate emissions(PE/PM) (formerlyparticulate matter, PM)

63.82 3.54 4.91 3.54 4.91

PM # 10 microns indiameter (PE/PM10)

27.12 1.51 1.74 1.51 1.74

PM # 2.5 microns indiameter (PE/PM2.5)

11.16 0.54 0.37 0.54 0.37

Sulfur dioxide (SO2) 0 0 0 0 0

Nitrogen oxides (NOx) 0 0 0 0 0

Carbon monoxide (CO) 0 0 0 0 0

Organic compounds (OC) 0 0 0 0 0

Volatile organiccompounds (VOC)

0 0 0 0 0

Lead (Pb) 0 0 0 0 0

Total Hazardous AirPollutants (HAPs)

0 0 0 0 0

Page 80: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

4.

5.

6.

7.

8.

9.

10.

IronUnits LLC - Toledo HBI - 0448011992 Page 2 PTI/PTIO Application - A0064540

Highest single HAP 0 0 0 0 0

Best Available Technology (BAT) - For each pollutant for which the Requested Allowable in the above table exceeds 10

tons per year, BAT, as defined in OAC 3745-31-01, is required. Describe what has been selected as BAT and the basis for

the selection:

Please see the PTI application that addresses BACT requirements that alsoconstitute BAT.

Control Equipment - Does this air contaminant source employ emissions control equipment?

See Facility Profile

Process Flow Diagram - Attach a Process Flow Diagram to this application for this air contaminant source. See the

application instructions for additional information.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694098 PFD forOxides andHBIUpdated

Processflowdiagram

X

Modeling information: (Note: items in bold in Tables 7-A and/or 7-B, as applicable, are required even if the tables do

not otherwise need to be completed. If applicable, all information is required An air quality modeling analysis is

required for PTIs and PTIOs for new installations or modifications, as defined in OAC rule 3745-31-01, where either the

increase of toxic air contaminants from any air contaminant source or the increase of any other pollutant for all air

contaminant sources combined exceed a threshold listed below. This analysis is to assure that the impact from the

requested project will not exceed Ohio's Acceptable Incremental Impacts for criteria pollutants and/or Maximum Allowable

Ground Level Concentrations (MAGLC) for toxic air contaminants. (See Ohio EPA, DAPC's Engineering Guide #69 for more

information.) Permit requests that would have unacceptable impacts cannot be approved as proposed. See the line-by-line

PTI/PTIO instructions for additional information.

See Facility Profile

Request for Federally Enforceable Limits - As part of this permit application, do you wish to propose voluntary restrictions

to limit emissions in order to avoid specific requirements listed below, (i.e., are you requesting federally enforceable limits to

obtain synthetic minor status)?

No

Continuous Emissions Monitoring - Does this air contaminant source utilize any continuous emissions monitoring (CEM)

equipment for indicating or demonstrating compliance? This does not include continuous parametric monitoring systems.

See Facility Profile

EAC Forms - The appropriate Emissions Activity Category (EAC) form(s) must be completed and attached for each air

contaminant source. At least one complete EAC form must be submitted for each air contaminant source for the application

to be considered complete. Refer to the list attached to the application instructions. Please indicate which EAC form

corresponds to this air contaminant source.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694105 EAC formfor HBIstoragepileUpdated

EAC 3112StoragePiles

X

694107 EAC formfor FELUpdated

EAC 3111Roadwaysand

X

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IronUnits LLC - Toledo HBI - 0448011992 Page 3 PTI/PTIO Application - A0064540

ParkingAreas

694108 EAC formfor oxide,lumps,fines,REMET,coatingUpdated

EAC 3113MaterialHandling

X

694109 EAC formfor oxidestoragepileUpdated

EAC 3112StoragePiles

X

694124 EAC formfor HBIUpdated

EAC 3113MaterialHandling

X

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1.

2.

3.

-

-

-

-

-

IronUnits LLC - Toledo HBI - 0448011992 Page 1 PTI/PTIO Application - A0064540

Section II - Specific Air Contaminant Source Information Facility ID: 0448011992Emissions Unit ID: P001

Company Equipment ID: TR-28b, P-1

One copy of this section should be filled out for each air contaminant source (emissions unit) covered by thisPTI/PTIO application identified in Section I, Question 5. See the application instructions for additional information.

Air Contaminant Source Installation or Modification Schedule - Check all that apply (must be completed regardless of

date of installation or modification):

New installation (for which construction has not yet begun, in accordance with OAC rule 3745-31-33). When will you beginto install the air contaminant source?after installation permit has been issued

SCC Codes - List all Source Classification Code(s) (SCC) that describe the process(es) performed by this air contaminant

source (e.g., 1-02-002-04).

See Facility Profile

Emissions Information - The following table requests information needed to determine the applicable requirements and the

compliance status of this air contaminant source with those requirements. Suggestions for how to estimate emissions may

be found in the instructions to the Emissions Activity Category (EAC) forms required with this application. If you need further

assistance, contact your District Office/Local Air Agency representative.

If total potential emissions of HAPs or any Toxic Air Contaminant (as identified in OAC rule 3745-114-01) are greater

than 1 ton/yr, fill in the table for that (those) pollutant(s). For all other pollutants, if “Emissions before controls (max),

lb/hr” multiplied by 24 hours/day is greater than 10 lbs/day, fill in the table for that pollutant.

Actual emissions are calculated including add-on control equipment. If you have no add-on control equipment,

“Emissions before controls” will be the same as “Actual emissions”.

Actual emissions and Requested Allowable should be based on operating 8760 hr/yr unless you are requesting federally

enforceable operating restrictions to limit emissions. If so, calculate emissions based on requested operating restrictions

and describe in your calculations.

If you use units other than lbs/hr or ton/yr, specify the units used (e.g., gr/dscf, lb/ton charged, lb/MMBtu, tons/12-

months).

Requested Allowable (ton/yr) is often equivalent to Potential to Emit (PTE) as defined in OAC rule 3745-31-01 and OAC

rule 3745-77-01.

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Particulate emissions(PE/PM) (formerlyparticulate matter, PM)

271.7 2.71 11.89 2.71 11.89

PM # 10 microns indiameter (PE/PM10)

271.7 2.71 11.89 2.71 11.89

PM # 2.5 microns indiameter (PE/PM2.5)

271.7 2.71 11.89 2.71 11.89

Sulfur dioxide (SO2) 0 0 0 0 0

Nitrogen oxides (NOx) 2.45 2.45 10.73 2.45 10.73

Carbon monoxide (CO) 988.85 988.85 4331.16 988.85 4331.16

Organic compounds (OC) 0 0 0 0 0

Volatile organiccompounds (VOC)

0 0 0 0 0

Lead (Pb) 0 0 0 0 0

Total Hazardous AirPollutants (HAPs)

0 0 0 0 0

Page 83: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

4.

5.

6.

7.

8.

9.

10.

IronUnits LLC - Toledo HBI - 0448011992 Page 2 PTI/PTIO Application - A0064540

Highest single HAP 0 0 0 0 0

Greenhouse Gas Pollutants:

Pollutant Emissionsbefore

controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

CO2e(ton/year)

Carbon Dioxide 2182 2182 9558 2182 9558 9,558

Best Available Technology (BAT) - For each pollutant for which the Requested Allowable in the above table exceeds 10

tons per year, BAT, as defined in OAC 3745-31-01, is required. Describe what has been selected as BAT and the basis for

the selection:

Please see the PTI application that addresses BACT requirements that alsoconstitute BAT.

Control Equipment - Does this air contaminant source employ emissions control equipment?

See Facility Profile

Process Flow Diagram - Attach a Process Flow Diagram to this application for this air contaminant source. See the

application instructions for additional information.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694097 Processflowdiagramfor CorePlantUpdated

Processflowdiagram

X

Modeling information: (Note: items in bold in Tables 7-A and/or 7-B, as applicable, are required even if the tables do

not otherwise need to be completed. If applicable, all information is required An air quality modeling analysis is

required for PTIs and PTIOs for new installations or modifications, as defined in OAC rule 3745-31-01, where either the

increase of toxic air contaminants from any air contaminant source or the increase of any other pollutant for all air

contaminant sources combined exceed a threshold listed below. This analysis is to assure that the impact from the

requested project will not exceed Ohio's Acceptable Incremental Impacts for criteria pollutants and/or Maximum Allowable

Ground Level Concentrations (MAGLC) for toxic air contaminants. (See Ohio EPA, DAPC's Engineering Guide #69 for more

information.) Permit requests that would have unacceptable impacts cannot be approved as proposed. See the line-by-line

PTI/PTIO instructions for additional information.

See Facility Profile

Request for Federally Enforceable Limits - As part of this permit application, do you wish to propose voluntary restrictions

to limit emissions in order to avoid specific requirements listed below, (i.e., are you requesting federally enforceable limits to

obtain synthetic minor status)?

No

Continuous Emissions Monitoring - Does this air contaminant source utilize any continuous emissions monitoring (CEM)

equipment for indicating or demonstrating compliance? This does not include continuous parametric monitoring systems.

See Facility Profile

EAC Forms - The appropriate Emissions Activity Category (EAC) form(s) must be completed and attached for each air

contaminant source. At least one complete EAC form must be submitted for each air contaminant source for the application

to be considered complete. Refer to the list attached to the application instructions. Please indicate which EAC form

corresponds to this air contaminant source.

Process Flow Diagrams:

Page 84: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

IronUnits LLC - Toledo HBI - 0448011992 Page 3 PTI/PTIO Application - A0064540

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694114 RevisedEAC FormP-1

EAC 3100Processoperation

X 11/14/2017

694115 EAC formfor TR-28ChargeHopper

EAC 3100Processoperation

X

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1.

2.

3.

-

-

-

-

-

IronUnits LLC - Toledo HBI - 0448011992 Page 1 PTI/PTIO Application - A0064540

Section II - Specific Air Contaminant Source Information Facility ID: 0448011992Emissions Unit ID: P002

Company Equipment ID: P-3

One copy of this section should be filled out for each air contaminant source (emissions unit) covered by thisPTI/PTIO application identified in Section I, Question 5. See the application instructions for additional information.

Air Contaminant Source Installation or Modification Schedule - Check all that apply (must be completed regardless of

date of installation or modification):

New installation (for which construction has not yet begun, in accordance with OAC rule 3745-31-33). When will you beginto install the air contaminant source?after installation permit has been issued

SCC Codes - List all Source Classification Code(s) (SCC) that describe the process(es) performed by this air contaminant

source (e.g., 1-02-002-04).

See Facility Profile

Emissions Information - The following table requests information needed to determine the applicable requirements and the

compliance status of this air contaminant source with those requirements. Suggestions for how to estimate emissions may

be found in the instructions to the Emissions Activity Category (EAC) forms required with this application. If you need further

assistance, contact your District Office/Local Air Agency representative.

If total potential emissions of HAPs or any Toxic Air Contaminant (as identified in OAC rule 3745-114-01) are greater

than 1 ton/yr, fill in the table for that (those) pollutant(s). For all other pollutants, if “Emissions before controls (max),

lb/hr” multiplied by 24 hours/day is greater than 10 lbs/day, fill in the table for that pollutant.

Actual emissions are calculated including add-on control equipment. If you have no add-on control equipment,

“Emissions before controls” will be the same as “Actual emissions”.

Actual emissions and Requested Allowable should be based on operating 8760 hr/yr unless you are requesting federally

enforceable operating restrictions to limit emissions. If so, calculate emissions based on requested operating restrictions

and describe in your calculations.

If you use units other than lbs/hr or ton/yr, specify the units used (e.g., gr/dscf, lb/ton charged, lb/MMBtu, tons/12-

months).

Requested Allowable (ton/yr) is often equivalent to Potential to Emit (PTE) as defined in OAC rule 3745-31-01 and OAC

rule 3745-77-01.

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Particulate emissions(PE/PM) (formerlyparticulate matter, PM)

410 4.10 17.96 4.10 17.96

PM # 10 microns indiameter (PE/PM10)

410 4.10 17.96 4.10 17.96

PM # 2.5 microns indiameter (PE/PM2.5)

410 4.10 17.96 4.10 17.96

Sulfur dioxide (SO2) 0 0 0 0 0

Nitrogen oxides (NOx) 3.94 3.94 17.25 3.94 17.25

Carbon monoxide (CO) 912.01 912.01 3994.62 912.01 3994.62

Organic compounds (OC) 0 0 0 0 0

Volatile organiccompounds (VOC)

0 0 0 0 0

Lead (Pb) 0 0 0 0 0

Total Hazardous AirPollutants (HAPs)

0 0 0 0 0

Page 86: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

4.

5.

6.

7.

8.

9.

10.

IronUnits LLC - Toledo HBI - 0448011992 Page 2 PTI/PTIO Application - A0064540

Highest single HAP 0 0 0 0 0

Greenhouse Gas Pollutants:

Pollutant Emissionsbefore

controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

CO2e(ton/year)

Carbon Dioxide 12345 12345 54071 12345 54071 54,071

Best Available Technology (BAT) - For each pollutant for which the Requested Allowable in the above table exceeds 10

tons per year, BAT, as defined in OAC 3745-31-01, is required. Describe what has been selected as BAT and the basis for

the selection:

Please see the PTI application that addresses BACT requirements that alsoconstitute BAT.

Control Equipment - Does this air contaminant source employ emissions control equipment?

See Facility Profile

Process Flow Diagram - Attach a Process Flow Diagram to this application for this air contaminant source. See the

application instructions for additional information.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694097 Processflowdiagramfor CorePlantUpdated

Processflowdiagram

X

Modeling information: (Note: items in bold in Tables 7-A and/or 7-B, as applicable, are required even if the tables do

not otherwise need to be completed. If applicable, all information is required An air quality modeling analysis is

required for PTIs and PTIOs for new installations or modifications, as defined in OAC rule 3745-31-01, where either the

increase of toxic air contaminants from any air contaminant source or the increase of any other pollutant for all air

contaminant sources combined exceed a threshold listed below. This analysis is to assure that the impact from the

requested project will not exceed Ohio's Acceptable Incremental Impacts for criteria pollutants and/or Maximum Allowable

Ground Level Concentrations (MAGLC) for toxic air contaminants. (See Ohio EPA, DAPC's Engineering Guide #69 for more

information.) Permit requests that would have unacceptable impacts cannot be approved as proposed. See the line-by-line

PTI/PTIO instructions for additional information.

See Facility Profile

Request for Federally Enforceable Limits - As part of this permit application, do you wish to propose voluntary restrictions

to limit emissions in order to avoid specific requirements listed below, (i.e., are you requesting federally enforceable limits to

obtain synthetic minor status)?

No

Continuous Emissions Monitoring - Does this air contaminant source utilize any continuous emissions monitoring (CEM)

equipment for indicating or demonstrating compliance? This does not include continuous parametric monitoring systems.

See Facility Profile

EAC Forms - The appropriate Emissions Activity Category (EAC) form(s) must be completed and attached for each air

contaminant source. At least one complete EAC form must be submitted for each air contaminant source for the application

to be considered complete. Refer to the list attached to the application instructions. Please indicate which EAC form

corresponds to this air contaminant source.

Process Flow Diagrams:

Page 87: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

IronUnits LLC - Toledo HBI - 0448011992 Page 3 PTI/PTIO Application - A0064540

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694101 EAC formfor P-3

EAC 3100Processoperation

X

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2.

3.

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IronUnits LLC - Toledo HBI - 0448011992 Page 1 PTI/PTIO Application - A0064540

Section II - Specific Air Contaminant Source Information Facility ID: 0448011992Emissions Unit ID: P003

Company Equipment ID: P-4

One copy of this section should be filled out for each air contaminant source (emissions unit) covered by thisPTI/PTIO application identified in Section I, Question 5. See the application instructions for additional information.

Air Contaminant Source Installation or Modification Schedule - Check all that apply (must be completed regardless of

date of installation or modification):

New installation (for which construction has not yet begun, in accordance with OAC rule 3745-31-33). When will you beginto install the air contaminant source?after installation permit has been issued

SCC Codes - List all Source Classification Code(s) (SCC) that describe the process(es) performed by this air contaminant

source (e.g., 1-02-002-04).

See Facility Profile

Emissions Information - The following table requests information needed to determine the applicable requirements and the

compliance status of this air contaminant source with those requirements. Suggestions for how to estimate emissions may

be found in the instructions to the Emissions Activity Category (EAC) forms required with this application. If you need further

assistance, contact your District Office/Local Air Agency representative.

If total potential emissions of HAPs or any Toxic Air Contaminant (as identified in OAC rule 3745-114-01) are greater

than 1 ton/yr, fill in the table for that (those) pollutant(s). For all other pollutants, if “Emissions before controls (max),

lb/hr” multiplied by 24 hours/day is greater than 10 lbs/day, fill in the table for that pollutant.

Actual emissions are calculated including add-on control equipment. If you have no add-on control equipment,

“Emissions before controls” will be the same as “Actual emissions”.

Actual emissions and Requested Allowable should be based on operating 8760 hr/yr unless you are requesting federally

enforceable operating restrictions to limit emissions. If so, calculate emissions based on requested operating restrictions

and describe in your calculations.

If you use units other than lbs/hr or ton/yr, specify the units used (e.g., gr/dscf, lb/ton charged, lb/MMBtu, tons/12-

months).

Requested Allowable (ton/yr) is often equivalent to Potential to Emit (PTE) as defined in OAC rule 3745-31-01 and OAC

rule 3745-77-01.

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Particulate emissions(PE/PM) (formerlyparticulate matter, PM)

380 3.80 16.64 3.80 16.64

PM # 10 microns indiameter (PE/PM10)

380 3.80 16.64 3.8 16.64

PM # 2.5 microns indiameter (PE/PM2.5)

380 3.80 16.64 3.8 16.64

Sulfur dioxide (SO2) 0 0 0 0 0

Nitrogen oxides (NOx) 0 0 0 0 0

Carbon monoxide (CO) 594.1 594.1 2602.1 594.1 2602.1

Organic compounds (OC) 0 0 0 0 0

Volatile organiccompounds (VOC)

0 0 0 0 0

Lead (Pb) 0 0 0 0 0

Total Hazardous AirPollutants (HAPs)

0 0 0 0 0

Page 89: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

4.

5.

6.

7.

8.

9.

10.

IronUnits LLC - Toledo HBI - 0448011992 Page 2 PTI/PTIO Application - A0064540

Highest single HAP 0 0 0 0 0

Best Available Technology (BAT) - For each pollutant for which the Requested Allowable in the above table exceeds 10

tons per year, BAT, as defined in OAC 3745-31-01, is required. Describe what has been selected as BAT and the basis for

the selection:

Please see the PTI application that addresses BACT requirements that alsoconstitute BAT.

Control Equipment - Does this air contaminant source employ emissions control equipment?

See Facility Profile

Process Flow Diagram - Attach a Process Flow Diagram to this application for this air contaminant source. See the

application instructions for additional information.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694097 Processflowdiagramfor CorePlantUpdated

Processflowdiagram

X

Modeling information: (Note: items in bold in Tables 7-A and/or 7-B, as applicable, are required even if the tables do

not otherwise need to be completed. If applicable, all information is required An air quality modeling analysis is

required for PTIs and PTIOs for new installations or modifications, as defined in OAC rule 3745-31-01, where either the

increase of toxic air contaminants from any air contaminant source or the increase of any other pollutant for all air

contaminant sources combined exceed a threshold listed below. This analysis is to assure that the impact from the

requested project will not exceed Ohio's Acceptable Incremental Impacts for criteria pollutants and/or Maximum Allowable

Ground Level Concentrations (MAGLC) for toxic air contaminants. (See Ohio EPA, DAPC's Engineering Guide #69 for more

information.) Permit requests that would have unacceptable impacts cannot be approved as proposed. See the line-by-line

PTI/PTIO instructions for additional information.

See Facility Profile

Request for Federally Enforceable Limits - As part of this permit application, do you wish to propose voluntary restrictions

to limit emissions in order to avoid specific requirements listed below, (i.e., are you requesting federally enforceable limits to

obtain synthetic minor status)?

No

Continuous Emissions Monitoring - Does this air contaminant source utilize any continuous emissions monitoring (CEM)

equipment for indicating or demonstrating compliance? This does not include continuous parametric monitoring systems.

See Facility Profile

EAC Forms - The appropriate Emissions Activity Category (EAC) form(s) must be completed and attached for each air

contaminant source. At least one complete EAC form must be submitted for each air contaminant source for the application

to be considered complete. Refer to the list attached to the application instructions. Please indicate which EAC form

corresponds to this air contaminant source.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694100 EAC formfor P-4

EAC 3100Processoperation

X

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1.

2.

3.

-

-

-

-

-

IronUnits LLC - Toledo HBI - 0448011992 Page 1 PTI/PTIO Application - A0064540

Section II - Specific Air Contaminant Source Information Facility ID: 0448011992Emissions Unit ID: P004

Company Equipment ID: P-5

One copy of this section should be filled out for each air contaminant source (emissions unit) covered by thisPTI/PTIO application identified in Section I, Question 5. See the application instructions for additional information.

Air Contaminant Source Installation or Modification Schedule - Check all that apply (must be completed regardless of

date of installation or modification):

New installation (for which construction has not yet begun, in accordance with OAC rule 3745-31-33). When will you beginto install the air contaminant source?after installation permit has been issued

SCC Codes - List all Source Classification Code(s) (SCC) that describe the process(es) performed by this air contaminant

source (e.g., 1-02-002-04).

See Facility Profile

Emissions Information - The following table requests information needed to determine the applicable requirements and the

compliance status of this air contaminant source with those requirements. Suggestions for how to estimate emissions may

be found in the instructions to the Emissions Activity Category (EAC) forms required with this application. If you need further

assistance, contact your District Office/Local Air Agency representative.

If total potential emissions of HAPs or any Toxic Air Contaminant (as identified in OAC rule 3745-114-01) are greater

than 1 ton/yr, fill in the table for that (those) pollutant(s). For all other pollutants, if “Emissions before controls (max),

lb/hr” multiplied by 24 hours/day is greater than 10 lbs/day, fill in the table for that pollutant.

Actual emissions are calculated including add-on control equipment. If you have no add-on control equipment,

“Emissions before controls” will be the same as “Actual emissions”.

Actual emissions and Requested Allowable should be based on operating 8760 hr/yr unless you are requesting federally

enforceable operating restrictions to limit emissions. If so, calculate emissions based on requested operating restrictions

and describe in your calculations.

If you use units other than lbs/hr or ton/yr, specify the units used (e.g., gr/dscf, lb/ton charged, lb/MMBtu, tons/12-

months).

Requested Allowable (ton/yr) is often equivalent to Potential to Emit (PTE) as defined in OAC rule 3745-31-01 and OAC

rule 3745-77-01.

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Particulate emissions(PE/PM) (formerlyparticulate matter, PM)

0 0 0 0 0

PM # 10 microns indiameter (PE/PM10)

0 0 0 0 0

PM # 2.5 microns indiameter (PE/PM2.5)

0 0 0 0 0

Sulfur dioxide (SO2) 0 0 0 0 0

Nitrogen oxides (NOx) 0 0 0 0 0

Carbon monoxide (CO) 110.1 110.1 482.1 110.1 482.1

Organic compounds (OC) 0 0 0 0 0

Volatile organiccompounds (VOC)

0 0 0 0 0

Lead (Pb) 0 0 0 0 0

Total Hazardous AirPollutants (HAPs)

0 0 0 0 0

Page 91: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

4.

5.

6.

7.

8.

9.

IronUnits LLC - Toledo HBI - 0448011992 Page 2 PTI/PTIO Application - A0064540

Highest single HAP 0 0 0 0 0

Hazardous Air Pollutants (HAPs):

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Ammonia 3.97 3.97 17.40 3.97 17.40

Greenhouse Gas Pollutants:

Pollutant Emissionsbefore

controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

CO2e(ton/year)

Carbon Dioxide 4122 4122 18054 4122 18054 18,054

Best Available Technology (BAT) - For each pollutant for which the Requested Allowable in the above table exceeds 10

tons per year, BAT, as defined in OAC 3745-31-01, is required. Describe what has been selected as BAT and the basis for

the selection:

Please see the PTI application that addresses BACT requirements that alsoconstitute BAT.

Control Equipment - Does this air contaminant source employ emissions control equipment?

See Facility Profile

Process Flow Diagram - Attach a Process Flow Diagram to this application for this air contaminant source. See the

application instructions for additional information.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694097 Processflowdiagramfor CorePlantUpdated

Processflowdiagram

X

Modeling information: (Note: items in bold in Tables 7-A and/or 7-B, as applicable, are required even if the tables do

not otherwise need to be completed. If applicable, all information is required An air quality modeling analysis is

required for PTIs and PTIOs for new installations or modifications, as defined in OAC rule 3745-31-01, where either the

increase of toxic air contaminants from any air contaminant source or the increase of any other pollutant for all air

contaminant sources combined exceed a threshold listed below. This analysis is to assure that the impact from the

requested project will not exceed Ohio's Acceptable Incremental Impacts for criteria pollutants and/or Maximum Allowable

Ground Level Concentrations (MAGLC) for toxic air contaminants. (See Ohio EPA, DAPC's Engineering Guide #69 for more

information.) Permit requests that would have unacceptable impacts cannot be approved as proposed. See the line-by-line

PTI/PTIO instructions for additional information.

See Facility Profile

Request for Federally Enforceable Limits - As part of this permit application, do you wish to propose voluntary restrictions

to limit emissions in order to avoid specific requirements listed below, (i.e., are you requesting federally enforceable limits to

obtain synthetic minor status)?

Not sure

Continuous Emissions Monitoring - Does this air contaminant source utilize any continuous emissions monitoring (CEM)

equipment for indicating or demonstrating compliance? This does not include continuous parametric monitoring systems.

See Facility Profile

Page 92: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

10.

IronUnits LLC - Toledo HBI - 0448011992 Page 3 PTI/PTIO Application - A0064540

EAC Forms - The appropriate Emissions Activity Category (EAC) form(s) must be completed and attached for each air

contaminant source. At least one complete EAC form must be submitted for each air contaminant source for the application

to be considered complete. Refer to the list attached to the application instructions. Please indicate which EAC form

corresponds to this air contaminant source.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694112 RevisedEAC FormP-5

EAC 3100Processoperation

X 11/14/2017

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1.

2.

3.

-

-

-

-

-

IronUnits LLC - Toledo HBI - 0448011992 Page 1 PTI/PTIO Application - A0064540

Section II - Specific Air Contaminant Source Information Facility ID: 0448011992Emissions Unit ID: P005

Company Equipment ID: P-7

One copy of this section should be filled out for each air contaminant source (emissions unit) covered by thisPTI/PTIO application identified in Section I, Question 5. See the application instructions for additional information.

Air Contaminant Source Installation or Modification Schedule - Check all that apply (must be completed regardless of

date of installation or modification):

New installation (for which construction has not yet begun, in accordance with OAC rule 3745-31-33). When will you beginto install the air contaminant source?after installation permit has been issued

SCC Codes - List all Source Classification Code(s) (SCC) that describe the process(es) performed by this air contaminant

source (e.g., 1-02-002-04).

See Facility Profile

Emissions Information - The following table requests information needed to determine the applicable requirements and the

compliance status of this air contaminant source with those requirements. Suggestions for how to estimate emissions may

be found in the instructions to the Emissions Activity Category (EAC) forms required with this application. If you need further

assistance, contact your District Office/Local Air Agency representative.

If total potential emissions of HAPs or any Toxic Air Contaminant (as identified in OAC rule 3745-114-01) are greater

than 1 ton/yr, fill in the table for that (those) pollutant(s). For all other pollutants, if “Emissions before controls (max),

lb/hr” multiplied by 24 hours/day is greater than 10 lbs/day, fill in the table for that pollutant.

Actual emissions are calculated including add-on control equipment. If you have no add-on control equipment,

“Emissions before controls” will be the same as “Actual emissions”.

Actual emissions and Requested Allowable should be based on operating 8760 hr/yr unless you are requesting federally

enforceable operating restrictions to limit emissions. If so, calculate emissions based on requested operating restrictions

and describe in your calculations.

If you use units other than lbs/hr or ton/yr, specify the units used (e.g., gr/dscf, lb/ton charged, lb/MMBtu, tons/12-

months).

Requested Allowable (ton/yr) is often equivalent to Potential to Emit (PTE) as defined in OAC rule 3745-31-01 and OAC

rule 3745-77-01.

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Particulate emissions(PE/PM) (formerlyparticulate matter, PM)

13.64 0.07 0.3 0.07 0.3

PM # 10 microns indiameter (PE/PM10)

4.3 0.02 0.09 0.02 0.09

PM # 2.5 microns indiameter (PE/PM2.5)

2.6 0.01 0.06 0.01 0.06

Sulfur dioxide (SO2) 0 0 0 0 0

Nitrogen oxides (NOx) 0 0 0 0 0

Carbon monoxide (CO) 0 0 0 0 0

Organic compounds (OC) 0 0 0 0 0

Volatile organiccompounds (VOC)

0 0 0 0 0

Lead (Pb) 0 0 0 0 0

Total Hazardous AirPollutants (HAPs)

0 0 0 0 0

Page 94: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

4.

5.

6.

7.

8.

9.

10.

IronUnits LLC - Toledo HBI - 0448011992 Page 2 PTI/PTIO Application - A0064540

Highest single HAP 0 0 0 0 0

Hazardous Air Pollutants (HAPs):

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Ammonia 2.25 2.25 9.86 2.25 9.86

Best Available Technology (BAT) - For each pollutant for which the Requested Allowable in the above table exceeds 10

tons per year, BAT, as defined in OAC 3745-31-01, is required. Describe what has been selected as BAT and the basis for

the selection:

Please see the PTI application that addresses BACT requirements that alsoconstitute BAT.

Control Equipment - Does this air contaminant source employ emissions control equipment?

See Facility Profile

Process Flow Diagram - Attach a Process Flow Diagram to this application for this air contaminant source. See the

application instructions for additional information.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694097 Processflowdiagramfor CorePlantUpdated

Processflowdiagram

X

Modeling information: (Note: items in bold in Tables 7-A and/or 7-B, as applicable, are required even if the tables do

not otherwise need to be completed. If applicable, all information is required An air quality modeling analysis is

required for PTIs and PTIOs for new installations or modifications, as defined in OAC rule 3745-31-01, where either the

increase of toxic air contaminants from any air contaminant source or the increase of any other pollutant for all air

contaminant sources combined exceed a threshold listed below. This analysis is to assure that the impact from the

requested project will not exceed Ohio's Acceptable Incremental Impacts for criteria pollutants and/or Maximum Allowable

Ground Level Concentrations (MAGLC) for toxic air contaminants. (See Ohio EPA, DAPC's Engineering Guide #69 for more

information.) Permit requests that would have unacceptable impacts cannot be approved as proposed. See the line-by-line

PTI/PTIO instructions for additional information.

See Facility Profile

Request for Federally Enforceable Limits - As part of this permit application, do you wish to propose voluntary restrictions

to limit emissions in order to avoid specific requirements listed below, (i.e., are you requesting federally enforceable limits to

obtain synthetic minor status)?

No

Continuous Emissions Monitoring - Does this air contaminant source utilize any continuous emissions monitoring (CEM)

equipment for indicating or demonstrating compliance? This does not include continuous parametric monitoring systems.

See Facility Profile

EAC Forms - The appropriate Emissions Activity Category (EAC) form(s) must be completed and attached for each air

contaminant source. At least one complete EAC form must be submitted for each air contaminant source for the application

to be considered complete. Refer to the list attached to the application instructions. Please indicate which EAC form

corresponds to this air contaminant source.

Process Flow Diagrams:

Attachment Attachment Description EAC Form Public Trade Secret Trade Secret Event Date

Page 95: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

IronUnits LLC - Toledo HBI - 0448011992 Page 3 PTI/PTIO Application - A0064540

ID Type Type Document Document Justification694110 Revised

CoolingTower EAC

EAC 3100Processoperation

X 09/13/2017

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1.

2.

3.

-

-

-

-

-

IronUnits LLC - Toledo HBI - 0448011992 Page 1 PTI/PTIO Application - A0064540

Section II - Specific Air Contaminant Source Information Facility ID: 0448011992Emissions Unit ID: P006

Company Equipment ID: P-8

One copy of this section should be filled out for each air contaminant source (emissions unit) covered by thisPTI/PTIO application identified in Section I, Question 5. See the application instructions for additional information.

Air Contaminant Source Installation or Modification Schedule - Check all that apply (must be completed regardless of

date of installation or modification):

New installation (for which construction has not yet begun, in accordance with OAC rule 3745-31-33). When will you beginto install the air contaminant source?after installation permit has been issued

SCC Codes - List all Source Classification Code(s) (SCC) that describe the process(es) performed by this air contaminant

source (e.g., 1-02-002-04).

See Facility Profile

Emissions Information - The following table requests information needed to determine the applicable requirements and the

compliance status of this air contaminant source with those requirements. Suggestions for how to estimate emissions may

be found in the instructions to the Emissions Activity Category (EAC) forms required with this application. If you need further

assistance, contact your District Office/Local Air Agency representative.

If total potential emissions of HAPs or any Toxic Air Contaminant (as identified in OAC rule 3745-114-01) are greater

than 1 ton/yr, fill in the table for that (those) pollutant(s). For all other pollutants, if “Emissions before controls (max),

lb/hr” multiplied by 24 hours/day is greater than 10 lbs/day, fill in the table for that pollutant.

Actual emissions are calculated including add-on control equipment. If you have no add-on control equipment,

“Emissions before controls” will be the same as “Actual emissions”.

Actual emissions and Requested Allowable should be based on operating 8760 hr/yr unless you are requesting federally

enforceable operating restrictions to limit emissions. If so, calculate emissions based on requested operating restrictions

and describe in your calculations.

If you use units other than lbs/hr or ton/yr, specify the units used (e.g., gr/dscf, lb/ton charged, lb/MMBtu, tons/12-

months).

Requested Allowable (ton/yr) is often equivalent to Potential to Emit (PTE) as defined in OAC rule 3745-31-01 and OAC

rule 3745-77-01.

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Particulate emissions(PE/PM) (formerlyparticulate matter, PM)

0 0 0 0 0

PM # 10 microns indiameter (PE/PM10)

0 0 0 0 0

PM # 2.5 microns indiameter (PE/PM2.5)

0 0 0 0 0

Sulfur dioxide (SO2) 0 0 0 0 0

Nitrogen oxides (NOx) 2.05 2.05 0.51 2.05 0.51

Carbon monoxide (CO) 1.79 1.79 0.45 1.79 0.45

Organic compounds (OC) 0 0 0 0 0

Volatile organiccompounds (VOC)

0 0 0 0 0

Lead (Pb) 0 0 0 0 0

Total Hazardous AirPollutants (HAPs)

0 0 0 0 0

Page 97: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

4.

5.

6.

7.

8.

9.

10.

IronUnits LLC - Toledo HBI - 0448011992 Page 2 PTI/PTIO Application - A0064540

Highest single HAP 0 0 0 0 0

Greenhouse Gas Pollutants:

Pollutant Emissionsbefore

controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

CO2e(ton/year)

Carbon Dioxide 394 394 98 394 98 98

Best Available Technology (BAT) - For each pollutant for which the Requested Allowable in the above table exceeds 10

tons per year, BAT, as defined in OAC 3745-31-01, is required. Describe what has been selected as BAT and the basis for

the selection:

Control Equipment - Does this air contaminant source employ emissions control equipment?

See Facility Profile

Process Flow Diagram - Attach a Process Flow Diagram to this application for this air contaminant source. See the

application instructions for additional information.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694097 Processflowdiagramfor CorePlantUpdated

Processflowdiagram

X

Modeling information: (Note: items in bold in Tables 7-A and/or 7-B, as applicable, are required even if the tables do

not otherwise need to be completed. If applicable, all information is required An air quality modeling analysis is

required for PTIs and PTIOs for new installations or modifications, as defined in OAC rule 3745-31-01, where either the

increase of toxic air contaminants from any air contaminant source or the increase of any other pollutant for all air

contaminant sources combined exceed a threshold listed below. This analysis is to assure that the impact from the

requested project will not exceed Ohio's Acceptable Incremental Impacts for criteria pollutants and/or Maximum Allowable

Ground Level Concentrations (MAGLC) for toxic air contaminants. (See Ohio EPA, DAPC's Engineering Guide #69 for more

information.) Permit requests that would have unacceptable impacts cannot be approved as proposed. See the line-by-line

PTI/PTIO instructions for additional information.

See Facility Profile

Request for Federally Enforceable Limits - As part of this permit application, do you wish to propose voluntary restrictions

to limit emissions in order to avoid specific requirements listed below, (i.e., are you requesting federally enforceable limits to

obtain synthetic minor status)?

No

Continuous Emissions Monitoring - Does this air contaminant source utilize any continuous emissions monitoring (CEM)

equipment for indicating or demonstrating compliance? This does not include continuous parametric monitoring systems.

See Facility Profile

EAC Forms - The appropriate Emissions Activity Category (EAC) form(s) must be completed and attached for each air

contaminant source. At least one complete EAC form must be submitted for each air contaminant source for the application

to be considered complete. Refer to the list attached to the application instructions. Please indicate which EAC form

corresponds to this air contaminant source.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

Page 98: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

IronUnits LLC - Toledo HBI - 0448011992 Page 3 PTI/PTIO Application - A0064540

694102 EAC formfor FirePumpUpdated

EAC 3862Stationary InternalCombustion Engine

X

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1.

2.

3.

-

-

-

-

-

IronUnits LLC - Toledo HBI - 0448011992 Page 1 PTI/PTIO Application - A0064540

Section II - Specific Air Contaminant Source Information Facility ID: 0448011992Emissions Unit ID: P007

Company Equipment ID: P-9

One copy of this section should be filled out for each air contaminant source (emissions unit) covered by thisPTI/PTIO application identified in Section I, Question 5. See the application instructions for additional information.

Air Contaminant Source Installation or Modification Schedule - Check all that apply (must be completed regardless of

date of installation or modification):

New installation (for which construction has not yet begun, in accordance with OAC rule 3745-31-33). When will you beginto install the air contaminant source?after installation permit has been issued

SCC Codes - List all Source Classification Code(s) (SCC) that describe the process(es) performed by this air contaminant

source (e.g., 1-02-002-04).

See Facility Profile

Emissions Information - The following table requests information needed to determine the applicable requirements and the

compliance status of this air contaminant source with those requirements. Suggestions for how to estimate emissions may

be found in the instructions to the Emissions Activity Category (EAC) forms required with this application. If you need further

assistance, contact your District Office/Local Air Agency representative.

If total potential emissions of HAPs or any Toxic Air Contaminant (as identified in OAC rule 3745-114-01) are greater

than 1 ton/yr, fill in the table for that (those) pollutant(s). For all other pollutants, if “Emissions before controls (max),

lb/hr” multiplied by 24 hours/day is greater than 10 lbs/day, fill in the table for that pollutant.

Actual emissions are calculated including add-on control equipment. If you have no add-on control equipment,

“Emissions before controls” will be the same as “Actual emissions”.

Actual emissions and Requested Allowable should be based on operating 8760 hr/yr unless you are requesting federally

enforceable operating restrictions to limit emissions. If so, calculate emissions based on requested operating restrictions

and describe in your calculations.

If you use units other than lbs/hr or ton/yr, specify the units used (e.g., gr/dscf, lb/ton charged, lb/MMBtu, tons/12-

months).

Requested Allowable (ton/yr) is often equivalent to Potential to Emit (PTE) as defined in OAC rule 3745-31-01 and OAC

rule 3745-77-01.

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Particulate emissions(PE/PM) (formerlyparticulate matter, PM)

1.01 1.01 0.25 1.01 0.25

PM # 10 microns indiameter (PE/PM10)

1.01 1.01 0.25 1.01 0.25

PM # 2.5 microns indiameter (PE/PM2.5)

1.01 1.01 0.25 1.01 0.25

Sulfur dioxide (SO2) 0 0 0 0 0

Nitrogen oxides (NOx) 28.22 28.22 7.05 28.22 7.05

Carbon monoxide (CO) 15.43 15.43 3.86 15.43 3.86

Organic compounds (OC) 1.72 1.72 0.43 1.72 0.43

Volatile organiccompounds (VOC)

1.72 1.72 0.43 1.72 0.43

Lead (Pb) 0 0 0 0 0

Total Hazardous AirPollutants (HAPs)

0 0 0 0 0

Page 100: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

4.

5.

6.

7.

8.

9.

10.

IronUnits LLC - Toledo HBI - 0448011992 Page 2 PTI/PTIO Application - A0064540

Highest single HAP 0 0 0 0 0

Greenhouse Gas Pollutants:

Pollutant Emissionsbefore

controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

CO2e(ton/year)

Carbon Dioxide 2723 2723 681 2723 681 681

Best Available Technology (BAT) - For each pollutant for which the Requested Allowable in the above table exceeds 10

tons per year, BAT, as defined in OAC 3745-31-01, is required. Describe what has been selected as BAT and the basis for

the selection:

Please see the PTI application that addresses BACT requirements that alsoconstitute BAT.

Control Equipment - Does this air contaminant source employ emissions control equipment?

See Facility Profile

Process Flow Diagram - Attach a Process Flow Diagram to this application for this air contaminant source. See the

application instructions for additional information.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694097 Processflowdiagramfor CorePlantUpdated

Processflowdiagram

X

Modeling information: (Note: items in bold in Tables 7-A and/or 7-B, as applicable, are required even if the tables do

not otherwise need to be completed. If applicable, all information is required An air quality modeling analysis is

required for PTIs and PTIOs for new installations or modifications, as defined in OAC rule 3745-31-01, where either the

increase of toxic air contaminants from any air contaminant source or the increase of any other pollutant for all air

contaminant sources combined exceed a threshold listed below. This analysis is to assure that the impact from the

requested project will not exceed Ohio's Acceptable Incremental Impacts for criteria pollutants and/or Maximum Allowable

Ground Level Concentrations (MAGLC) for toxic air contaminants. (See Ohio EPA, DAPC's Engineering Guide #69 for more

information.) Permit requests that would have unacceptable impacts cannot be approved as proposed. See the line-by-line

PTI/PTIO instructions for additional information.

See Facility Profile

Request for Federally Enforceable Limits - As part of this permit application, do you wish to propose voluntary restrictions

to limit emissions in order to avoid specific requirements listed below, (i.e., are you requesting federally enforceable limits to

obtain synthetic minor status)?

No

Continuous Emissions Monitoring - Does this air contaminant source utilize any continuous emissions monitoring (CEM)

equipment for indicating or demonstrating compliance? This does not include continuous parametric monitoring systems.

See Facility Profile

EAC Forms - The appropriate Emissions Activity Category (EAC) form(s) must be completed and attached for each air

contaminant source. At least one complete EAC form must be submitted for each air contaminant source for the application

to be considered complete. Refer to the list attached to the application instructions. Please indicate which EAC form

corresponds to this air contaminant source.

Process Flow Diagrams:

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IronUnits LLC - Toledo HBI - 0448011992 Page 3 PTI/PTIO Application - A0064540

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694096 EmergencyGeneratorrevisedEAC

EAC 3862Stationary InternalCombustion Engine

X 09/13/2017

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1.

2.

3.

-

-

-

-

-

IronUnits LLC - Toledo HBI - 0448011992 Page 1 PTI/PTIO Application - A0064540

Section II - Specific Air Contaminant Source Information Facility ID: 0448011992Emissions Unit ID: P008

Company Equipment ID: P-6

One copy of this section should be filled out for each air contaminant source (emissions unit) covered by thisPTI/PTIO application identified in Section I, Question 5. See the application instructions for additional information.

Air Contaminant Source Installation or Modification Schedule - Check all that apply (must be completed regardless of

date of installation or modification):

New installation (for which construction has not yet begun, in accordance with OAC rule 3745-31-33). When will you beginto install the air contaminant source?after installation permit has been issued

SCC Codes - List all Source Classification Code(s) (SCC) that describe the process(es) performed by this air contaminant

source (e.g., 1-02-002-04).

See Facility Profile

Emissions Information - The following table requests information needed to determine the applicable requirements and the

compliance status of this air contaminant source with those requirements. Suggestions for how to estimate emissions may

be found in the instructions to the Emissions Activity Category (EAC) forms required with this application. If you need further

assistance, contact your District Office/Local Air Agency representative.

If total potential emissions of HAPs or any Toxic Air Contaminant (as identified in OAC rule 3745-114-01) are greater

than 1 ton/yr, fill in the table for that (those) pollutant(s). For all other pollutants, if “Emissions before controls (max),

lb/hr” multiplied by 24 hours/day is greater than 10 lbs/day, fill in the table for that pollutant.

Actual emissions are calculated including add-on control equipment. If you have no add-on control equipment,

“Emissions before controls” will be the same as “Actual emissions”.

Actual emissions and Requested Allowable should be based on operating 8760 hr/yr unless you are requesting federally

enforceable operating restrictions to limit emissions. If so, calculate emissions based on requested operating restrictions

and describe in your calculations.

If you use units other than lbs/hr or ton/yr, specify the units used (e.g., gr/dscf, lb/ton charged, lb/MMBtu, tons/12-

months).

Requested Allowable (ton/yr) is often equivalent to Potential to Emit (PTE) as defined in OAC rule 3745-31-01 and OAC

rule 3745-77-01.

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Particulate emissions(PE/PM) (formerlyparticulate matter, PM)

0 0 0 0 0

PM # 10 microns indiameter (PE/PM10)

0 0 0 0 0

PM # 2.5 microns indiameter (PE/PM2.5)

0 0 0 0 0

Sulfur dioxide (SO2) 0 0 0 0 0

Nitrogen oxides (NOx) 1.38 1.38 6.05 1.38 6.05

Carbon monoxide (CO) 6.29 6.29 27.57 6.29 27.57

Organic compounds (OC) 1.05 1.05 4.6 1.05 4.6

Volatile organiccompounds (VOC)

1.05 1.05 4.6 1.05 4.6

Lead (Pb) 0 0 0 0 0

Total Hazardous AirPollutants (HAPs)

0 0 0 0 0

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4.

5.

6.

7.

8.

9.

10.

IronUnits LLC - Toledo HBI - 0448011992 Page 2 PTI/PTIO Application - A0064540

Highest single HAP 0 0 0 0 0

Greenhouse Gas Pollutants:

Pollutant Emissionsbefore

controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

CO2e(ton/year)

Carbon Dioxide 2375 2375 10402 2375 10402 10,402

Best Available Technology (BAT) - For each pollutant for which the Requested Allowable in the above table exceeds 10

tons per year, BAT, as defined in OAC 3745-31-01, is required. Describe what has been selected as BAT and the basis for

the selection:

Please see the PTI application that addresses BACT requirements that alsoconstitute BAT.

Control Equipment - Does this air contaminant source employ emissions control equipment?

See Facility Profile

Process Flow Diagram - Attach a Process Flow Diagram to this application for this air contaminant source. See the

application instructions for additional information.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694097 Processflowdiagramfor CorePlantUpdated

Processflowdiagram

X

Modeling information: (Note: items in bold in Tables 7-A and/or 7-B, as applicable, are required even if the tables do

not otherwise need to be completed. If applicable, all information is required An air quality modeling analysis is

required for PTIs and PTIOs for new installations or modifications, as defined in OAC rule 3745-31-01, where either the

increase of toxic air contaminants from any air contaminant source or the increase of any other pollutant for all air

contaminant sources combined exceed a threshold listed below. This analysis is to assure that the impact from the

requested project will not exceed Ohio's Acceptable Incremental Impacts for criteria pollutants and/or Maximum Allowable

Ground Level Concentrations (MAGLC) for toxic air contaminants. (See Ohio EPA, DAPC's Engineering Guide #69 for more

information.) Permit requests that would have unacceptable impacts cannot be approved as proposed. See the line-by-line

PTI/PTIO instructions for additional information.

See Facility Profile

Request for Federally Enforceable Limits - As part of this permit application, do you wish to propose voluntary restrictions

to limit emissions in order to avoid specific requirements listed below, (i.e., are you requesting federally enforceable limits to

obtain synthetic minor status)?

No

Continuous Emissions Monitoring - Does this air contaminant source utilize any continuous emissions monitoring (CEM)

equipment for indicating or demonstrating compliance? This does not include continuous parametric monitoring systems.

See Facility Profile

EAC Forms - The appropriate Emissions Activity Category (EAC) form(s) must be completed and attached for each air

contaminant source. At least one complete EAC form must be submitted for each air contaminant source for the application

to be considered complete. Refer to the list attached to the application instructions. Please indicate which EAC form

corresponds to this air contaminant source.

Process Flow Diagrams:

Page 104: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

IronUnits LLC - Toledo HBI - 0448011992 Page 3 PTI/PTIO Application - A0064540

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694116 RevisedEAC Form

EAC 3100Processoperation

X 11/14/2017

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1.

2.

3.

-

-

-

-

-

IronUnits LLC - Toledo HBI - 0448011992 Page 1 PTI/PTIO Application - A0064540

Section II - Specific Air Contaminant Source Information Facility ID: 0448011992Emissions Unit ID: P009

Company Equipment ID: P-10

One copy of this section should be filled out for each air contaminant source (emissions unit) covered by thisPTI/PTIO application identified in Section I, Question 5. See the application instructions for additional information.

Air Contaminant Source Installation or Modification Schedule - Check all that apply (must be completed regardless of

date of installation or modification):

New installation (for which construction has not yet begun, in accordance with OAC rule 3745-31-33). When will you beginto install the air contaminant source?after installation permit has been issued

SCC Codes - List all Source Classification Code(s) (SCC) that describe the process(es) performed by this air contaminant

source (e.g., 1-02-002-04).

See Facility Profile

Emissions Information - The following table requests information needed to determine the applicable requirements and the

compliance status of this air contaminant source with those requirements. Suggestions for how to estimate emissions may

be found in the instructions to the Emissions Activity Category (EAC) forms required with this application. If you need further

assistance, contact your District Office/Local Air Agency representative.

If total potential emissions of HAPs or any Toxic Air Contaminant (as identified in OAC rule 3745-114-01) are greater

than 1 ton/yr, fill in the table for that (those) pollutant(s). For all other pollutants, if “Emissions before controls (max),

lb/hr” multiplied by 24 hours/day is greater than 10 lbs/day, fill in the table for that pollutant.

Actual emissions are calculated including add-on control equipment. If you have no add-on control equipment,

“Emissions before controls” will be the same as “Actual emissions”.

Actual emissions and Requested Allowable should be based on operating 8760 hr/yr unless you are requesting federally

enforceable operating restrictions to limit emissions. If so, calculate emissions based on requested operating restrictions

and describe in your calculations.

If you use units other than lbs/hr or ton/yr, specify the units used (e.g., gr/dscf, lb/ton charged, lb/MMBtu, tons/12-

months).

Requested Allowable (ton/yr) is often equivalent to Potential to Emit (PTE) as defined in OAC rule 3745-31-01 and OAC

rule 3745-77-01.

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Particulate emissions(PE/PM) (formerlyparticulate matter, PM)

0 0 0 0 0

PM # 10 microns indiameter (PE/PM10)

0 0 0 0 0

PM # 2.5 microns indiameter (PE/PM2.5)

0 0 0 0 0

Sulfur dioxide (SO2) 0 0 0 0 0

Nitrogen oxides (NOx) 1 1 0.5 1 0.5

Carbon monoxide (CO) 1.1 1.1 0.5 1.1 0.5

Organic compounds (OC) 0 0 0 0 0

Volatile organiccompounds (VOC)

0 0 0 0 0

Lead (Pb) 0 0 0 0 0

Total Hazardous AirPollutants (HAPs)

0 0 0 0 0

Page 106: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

4.

5.

6.

7.

8.

9.

10.

IronUnits LLC - Toledo HBI - 0448011992 Page 2 PTI/PTIO Application - A0064540

Highest single HAP 0 0 0 0 0

Greenhouse Gas Pollutants:

Pollutant Emissionsbefore

controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

CO2e(ton/year)

Carbon Dioxide 155 155 39 155 39 39

Best Available Technology (BAT) - For each pollutant for which the Requested Allowable in the above table exceeds 10

tons per year, BAT, as defined in OAC 3745-31-01, is required. Describe what has been selected as BAT and the basis for

the selection:

Control Equipment - Does this air contaminant source employ emissions control equipment?

See Facility Profile

Process Flow Diagram - Attach a Process Flow Diagram to this application for this air contaminant source. See the

application instructions for additional information.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694097 Processflowdiagramfor CorePlantUpdated

Processflowdiagram

X

Modeling information: (Note: items in bold in Tables 7-A and/or 7-B, as applicable, are required even if the tables do

not otherwise need to be completed. If applicable, all information is required An air quality modeling analysis is

required for PTIs and PTIOs for new installations or modifications, as defined in OAC rule 3745-31-01, where either the

increase of toxic air contaminants from any air contaminant source or the increase of any other pollutant for all air

contaminant sources combined exceed a threshold listed below. This analysis is to assure that the impact from the

requested project will not exceed Ohio's Acceptable Incremental Impacts for criteria pollutants and/or Maximum Allowable

Ground Level Concentrations (MAGLC) for toxic air contaminants. (See Ohio EPA, DAPC's Engineering Guide #69 for more

information.) Permit requests that would have unacceptable impacts cannot be approved as proposed. See the line-by-line

PTI/PTIO instructions for additional information.

See Facility Profile

Request for Federally Enforceable Limits - As part of this permit application, do you wish to propose voluntary restrictions

to limit emissions in order to avoid specific requirements listed below, (i.e., are you requesting federally enforceable limits to

obtain synthetic minor status)?

Not sure

Continuous Emissions Monitoring - Does this air contaminant source utilize any continuous emissions monitoring (CEM)

equipment for indicating or demonstrating compliance? This does not include continuous parametric monitoring systems.

See Facility Profile

EAC Forms - The appropriate Emissions Activity Category (EAC) form(s) must be completed and attached for each air

contaminant source. At least one complete EAC form must be submitted for each air contaminant source for the application

to be considered complete. Refer to the list attached to the application instructions. Please indicate which EAC form

corresponds to this air contaminant source.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

Page 107: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

IronUnits LLC - Toledo HBI - 0448011992 Page 3 PTI/PTIO Application - A0064540

694111 EAC formfor AdminEmergencyGenerator

EAC 3862Stationary InternalCombustion Engine

X

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1.

2.

3.

-

-

-

-

-

IronUnits LLC - Toledo HBI - 0448011992 Page 1 PTI/PTIO Application - A0064540

Section II - Specific Air Contaminant Source Information Facility ID: 0448011992Emissions Unit ID: P901

Company Equipment ID: MTR-5,TR-1,TR-2,TR-5,TR-6,TR-7,TR10,SR1,TR13a,TR-13b,TR14

One copy of this section should be filled out for each air contaminant source (emissions unit) covered by thisPTI/PTIO application identified in Section I, Question 5. See the application instructions for additional information.

Air Contaminant Source Installation or Modification Schedule - Check all that apply (must be completed regardless of

date of installation or modification):

New installation (for which construction has not yet begun, in accordance with OAC rule 3745-31-33). When will you beginto install the air contaminant source?after installation permit has been issued

SCC Codes - List all Source Classification Code(s) (SCC) that describe the process(es) performed by this air contaminant

source (e.g., 1-02-002-04).

See Facility Profile

Emissions Information - The following table requests information needed to determine the applicable requirements and the

compliance status of this air contaminant source with those requirements. Suggestions for how to estimate emissions may

be found in the instructions to the Emissions Activity Category (EAC) forms required with this application. If you need further

assistance, contact your District Office/Local Air Agency representative.

If total potential emissions of HAPs or any Toxic Air Contaminant (as identified in OAC rule 3745-114-01) are greater

than 1 ton/yr, fill in the table for that (those) pollutant(s). For all other pollutants, if “Emissions before controls (max),

lb/hr” multiplied by 24 hours/day is greater than 10 lbs/day, fill in the table for that pollutant.

Actual emissions are calculated including add-on control equipment. If you have no add-on control equipment,

“Emissions before controls” will be the same as “Actual emissions”.

Actual emissions and Requested Allowable should be based on operating 8760 hr/yr unless you are requesting federally

enforceable operating restrictions to limit emissions. If so, calculate emissions based on requested operating restrictions

and describe in your calculations.

If you use units other than lbs/hr or ton/yr, specify the units used (e.g., gr/dscf, lb/ton charged, lb/MMBtu, tons/12-

months).

Requested Allowable (ton/yr) is often equivalent to Potential to Emit (PTE) as defined in OAC rule 3745-31-01 and OAC

rule 3745-77-01.

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Particulate emissions(PE/PM) (formerlyparticulate matter, PM)

134.57 2.5 5.0 2.5 5

PM # 10 microns indiameter (PE/PM10)

134 1.9 4.6 1.9 4.6

PM # 2.5 microns indiameter (PE/PM2.5)

133.49 1.4 4.3 1.4 4.3

Sulfur dioxide (SO2) 0 0 0 0 0

Nitrogen oxides (NOx) 0 0 0 0 0

Carbon monoxide (CO) 0 0 0 0 0

Organic compounds (OC) 0 0 0 0 0

Volatile organiccompounds (VOC)

0 0 0 0 0

Lead (Pb) 0 0 0 0 0

Page 109: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

4.

5.

6.

7.

8.

9.

10.

IronUnits LLC - Toledo HBI - 0448011992 Page 2 PTI/PTIO Application - A0064540

Total Hazardous AirPollutants (HAPs)

0 0 0 0 0

Highest single HAP 0 0 0 0 0

Best Available Technology (BAT) - For each pollutant for which the Requested Allowable in the above table exceeds 10

tons per year, BAT, as defined in OAC 3745-31-01, is required. Describe what has been selected as BAT and the basis for

the selection:

Please see the PTI application that addresses BACT requirements that alsoconstitute BAT.

Control Equipment - Does this air contaminant source employ emissions control equipment?

See Facility Profile

Process Flow Diagram - Attach a Process Flow Diagram to this application for this air contaminant source. See the

application instructions for additional information.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694098 PFD forOxides andHBIUpdated

Processflowdiagram

X

Modeling information: (Note: items in bold in Tables 7-A and/or 7-B, as applicable, are required even if the tables do

not otherwise need to be completed. If applicable, all information is required An air quality modeling analysis is

required for PTIs and PTIOs for new installations or modifications, as defined in OAC rule 3745-31-01, where either the

increase of toxic air contaminants from any air contaminant source or the increase of any other pollutant for all air

contaminant sources combined exceed a threshold listed below. This analysis is to assure that the impact from the

requested project will not exceed Ohio's Acceptable Incremental Impacts for criteria pollutants and/or Maximum Allowable

Ground Level Concentrations (MAGLC) for toxic air contaminants. (See Ohio EPA, DAPC's Engineering Guide #69 for more

information.) Permit requests that would have unacceptable impacts cannot be approved as proposed. See the line-by-line

PTI/PTIO instructions for additional information.

See Facility Profile

Request for Federally Enforceable Limits - As part of this permit application, do you wish to propose voluntary restrictions

to limit emissions in order to avoid specific requirements listed below, (i.e., are you requesting federally enforceable limits to

obtain synthetic minor status)?

No

Continuous Emissions Monitoring - Does this air contaminant source utilize any continuous emissions monitoring (CEM)

equipment for indicating or demonstrating compliance? This does not include continuous parametric monitoring systems.

See Facility Profile

EAC Forms - The appropriate Emissions Activity Category (EAC) form(s) must be completed and attached for each air

contaminant source. At least one complete EAC form must be submitted for each air contaminant source for the application

to be considered complete. Refer to the list attached to the application instructions. Please indicate which EAC form

corresponds to this air contaminant source.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694117 EAC formfor oxide,lumps,fines,REMET,coating

EAC 3113MaterialHandling

X

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IronUnits LLC - Toledo HBI - 0448011992 Page 3 PTI/PTIO Application - A0064540

Updated

Page 111: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

1.

2.

3.

-

-

-

-

-

IronUnits LLC - Toledo HBI - 0448011992 Page 1 PTI/PTIO Application - A0064540

Section II - Specific Air Contaminant Source Information Facility ID: 0448011992Emissions Unit ID: P902

Company Equipment ID: TR-17,TR-18,TR-19,TR-21b,TR-22,TR-23,TR-24,TR-25,TR-26,TR-27

One copy of this section should be filled out for each air contaminant source (emissions unit) covered by thisPTI/PTIO application identified in Section I, Question 5. See the application instructions for additional information.

Air Contaminant Source Installation or Modification Schedule - Check all that apply (must be completed regardless of

date of installation or modification):

New installation (for which construction has not yet begun, in accordance with OAC rule 3745-31-33). When will you beginto install the air contaminant source?after installation permit has been issued

SCC Codes - List all Source Classification Code(s) (SCC) that describe the process(es) performed by this air contaminant

source (e.g., 1-02-002-04).

See Facility Profile

Emissions Information - The following table requests information needed to determine the applicable requirements and the

compliance status of this air contaminant source with those requirements. Suggestions for how to estimate emissions may

be found in the instructions to the Emissions Activity Category (EAC) forms required with this application. If you need further

assistance, contact your District Office/Local Air Agency representative.

If total potential emissions of HAPs or any Toxic Air Contaminant (as identified in OAC rule 3745-114-01) are greater

than 1 ton/yr, fill in the table for that (those) pollutant(s). For all other pollutants, if “Emissions before controls (max),

lb/hr” multiplied by 24 hours/day is greater than 10 lbs/day, fill in the table for that pollutant.

Actual emissions are calculated including add-on control equipment. If you have no add-on control equipment,

“Emissions before controls” will be the same as “Actual emissions”.

Actual emissions and Requested Allowable should be based on operating 8760 hr/yr unless you are requesting federally

enforceable operating restrictions to limit emissions. If so, calculate emissions based on requested operating restrictions

and describe in your calculations.

If you use units other than lbs/hr or ton/yr, specify the units used (e.g., gr/dscf, lb/ton charged, lb/MMBtu, tons/12-

months).

Requested Allowable (ton/yr) is often equivalent to Potential to Emit (PTE) as defined in OAC rule 3745-31-01 and OAC

rule 3745-77-01.

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Particulate emissions(PE/PM) (formerlyparticulate matter, PM)

92.72 1.29 2.71 1.29 2.71

PM # 10 microns indiameter (PE/PM10)

54.69 0.6 1.66 0.6 1.66

PM # 2.5 microns indiameter (PE/PM2.5)

50.62 0.53 1.55 0.53 1.55

Sulfur dioxide (SO2) 0 0 0 0 0

Nitrogen oxides (NOx) 0 0 0 0 0

Carbon monoxide (CO) 0 0 0 0 0

Organic compounds (OC) 0 0 0 0 0

Volatile organiccompounds (VOC)

0 0 0 0 0

Lead (Pb) 0 0 0 0 0

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4.

5.

6.

7.

8.

9.

10.

IronUnits LLC - Toledo HBI - 0448011992 Page 2 PTI/PTIO Application - A0064540

Total Hazardous AirPollutants (HAPs)

0 0 0 0 0

Highest single HAP 0 0 0 0 0

Best Available Technology (BAT) - For each pollutant for which the Requested Allowable in the above table exceeds 10

tons per year, BAT, as defined in OAC 3745-31-01, is required. Describe what has been selected as BAT and the basis for

the selection:

Please see the PTI application that addresses BACT requirements that alsoconstitute BAT.

Control Equipment - Does this air contaminant source employ emissions control equipment?

See Facility Profile

Process Flow Diagram - Attach a Process Flow Diagram to this application for this air contaminant source. See the

application instructions for additional information.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694098 PFD forOxides andHBIUpdated

Processflowdiagram

X

Modeling information: (Note: items in bold in Tables 7-A and/or 7-B, as applicable, are required even if the tables do

not otherwise need to be completed. If applicable, all information is required An air quality modeling analysis is

required for PTIs and PTIOs for new installations or modifications, as defined in OAC rule 3745-31-01, where either the

increase of toxic air contaminants from any air contaminant source or the increase of any other pollutant for all air

contaminant sources combined exceed a threshold listed below. This analysis is to assure that the impact from the

requested project will not exceed Ohio's Acceptable Incremental Impacts for criteria pollutants and/or Maximum Allowable

Ground Level Concentrations (MAGLC) for toxic air contaminants. (See Ohio EPA, DAPC's Engineering Guide #69 for more

information.) Permit requests that would have unacceptable impacts cannot be approved as proposed. See the line-by-line

PTI/PTIO instructions for additional information.

See Facility Profile

Request for Federally Enforceable Limits - As part of this permit application, do you wish to propose voluntary restrictions

to limit emissions in order to avoid specific requirements listed below, (i.e., are you requesting federally enforceable limits to

obtain synthetic minor status)?

No

Continuous Emissions Monitoring - Does this air contaminant source utilize any continuous emissions monitoring (CEM)

equipment for indicating or demonstrating compliance? This does not include continuous parametric monitoring systems.

See Facility Profile

EAC Forms - The appropriate Emissions Activity Category (EAC) form(s) must be completed and attached for each air

contaminant source. At least one complete EAC form must be submitted for each air contaminant source for the application

to be considered complete. Refer to the list attached to the application instructions. Please indicate which EAC form

corresponds to this air contaminant source.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

695589 EAC formfor HBIhandlingandtransfersUpdated

EAC 3113MaterialHandling

X

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1.

2.

3.

-

-

-

-

-

IronUnits LLC - Toledo HBI - 0448011992 Page 3 PTI/PTIO Application - A0064540

Section II - Specific Air Contaminant Source Information Facility ID: 0448011992Emissions Unit ID: TMP213487

Company Equipment ID: Equip Leaks fromValves andConnectors

One copy of this section should be filled out for each air contaminant source (emissions unit) covered by thisPTI/PTIO application identified in Section I, Question 5. See the application instructions for additional information.

Air Contaminant Source Installation or Modification Schedule - Check all that apply (must be completed regardless of

date of installation or modification):

New installation (for which construction has not yet begun, in accordance with OAC rule 3745-31-33). When will you beginto install the air contaminant source?after installation permit has been issued

SCC Codes - List all Source Classification Code(s) (SCC) that describe the process(es) performed by this air contaminant

source (e.g., 1-02-002-04).

See Facility Profile

Emissions Information - The following table requests information needed to determine the applicable requirements and the

compliance status of this air contaminant source with those requirements. Suggestions for how to estimate emissions may

be found in the instructions to the Emissions Activity Category (EAC) forms required with this application. If you need further

assistance, contact your District Office/Local Air Agency representative.

If total potential emissions of HAPs or any Toxic Air Contaminant (as identified in OAC rule 3745-114-01) are greater

than 1 ton/yr, fill in the table for that (those) pollutant(s). For all other pollutants, if “Emissions before controls (max),

lb/hr” multiplied by 24 hours/day is greater than 10 lbs/day, fill in the table for that pollutant.

Actual emissions are calculated including add-on control equipment. If you have no add-on control equipment,

“Emissions before controls” will be the same as “Actual emissions”.

Actual emissions and Requested Allowable should be based on operating 8760 hr/yr unless you are requesting federally

enforceable operating restrictions to limit emissions. If so, calculate emissions based on requested operating restrictions

and describe in your calculations.

If you use units other than lbs/hr or ton/yr, specify the units used (e.g., gr/dscf, lb/ton charged, lb/MMBtu, tons/12-

months).

Requested Allowable (ton/yr) is often equivalent to Potential to Emit (PTE) as defined in OAC rule 3745-31-01 and OAC

rule 3745-77-01.

Pollutant Emissionsbefore controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

Particulate emissions(PE/PM) (formerlyparticulate matter, PM)

0 0 0 0 0

PM # 10 microns indiameter (PE/PM10)

0 0 0 0 0

PM # 2.5 microns indiameter (PE/PM2.5)

0 0 0 0 0

Sulfur dioxide (SO2) 0 0 0 0 0

Nitrogen oxides (NOx) 0 0 0 0 0

Carbon monoxide (CO) 0 0 0 0 0

Organic compounds (OC) 0.7 0.7 3.1 0.7 3.1

Volatile organiccompounds (VOC)

0.7 0.7 3.1 0.7 3.1

Lead (Pb) 0 0 0 0 0

Total Hazardous Air 0 0 0 0 0

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4.

5.

6.

7.

8.

9.

10.

IronUnits LLC - Toledo HBI - 0448011992 Page 1 PTI/PTIO Application - A0064540

Pollutants (HAPs)

Highest single HAP 0 0 0 0 0

Greenhouse Gas Pollutants:

Pollutant Emissionsbefore

controls(max)* (lb/hr)

Actualemissions

(lb/hr)

Actualemissions(ton/year)

RequestedAllowable

(lb/hr)

RequestedAllowable(ton/year)

CO2e(ton/year)

Methane 25.2 25.2 110.3 25.2 110.3 2,316.3

Best Available Technology (BAT) - For each pollutant for which the Requested Allowable in the above table exceeds 10

tons per year, BAT, as defined in OAC 3745-31-01, is required. Describe what has been selected as BAT and the basis for

the selection:

Control Equipment - Does this air contaminant source employ emissions control equipment?

See Facility Profile

Process Flow Diagram - Attach a Process Flow Diagram to this application for this air contaminant source. See the

application instructions for additional information.

Process Flow Diagrams:

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694097 Processflowdiagramfor CorePlantUpdated

Processflowdiagram

X

Modeling information: (Note: items in bold in Tables 7-A and/or 7-B, as applicable, are required even if the tables do

not otherwise need to be completed. If applicable, all information is required An air quality modeling analysis is

required for PTIs and PTIOs for new installations or modifications, as defined in OAC rule 3745-31-01, where either the

increase of toxic air contaminants from any air contaminant source or the increase of any other pollutant for all air

contaminant sources combined exceed a threshold listed below. This analysis is to assure that the impact from the

requested project will not exceed Ohio's Acceptable Incremental Impacts for criteria pollutants and/or Maximum Allowable

Ground Level Concentrations (MAGLC) for toxic air contaminants. (See Ohio EPA, DAPC's Engineering Guide #69 for more

information.) Permit requests that would have unacceptable impacts cannot be approved as proposed. See the line-by-line

PTI/PTIO instructions for additional information.

See Facility Profile

Request for Federally Enforceable Limits - As part of this permit application, do you wish to propose voluntary restrictions

to limit emissions in order to avoid specific requirements listed below, (i.e., are you requesting federally enforceable limits to

obtain synthetic minor status)?

No

Continuous Emissions Monitoring - Does this air contaminant source utilize any continuous emissions monitoring (CEM)

equipment for indicating or demonstrating compliance? This does not include continuous parametric monitoring systems.

See Facility Profile

EAC Forms - The appropriate Emissions Activity Category (EAC) form(s) must be completed and attached for each air

contaminant source. At least one complete EAC form must be submitted for each air contaminant source for the application

to be considered complete. Refer to the list attached to the application instructions. Please indicate which EAC form

corresponds to this air contaminant source.

Process Flow Diagrams:

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IronUnits LLC - Toledo HBI - 0448011992 Page 2 PTI/PTIO Application - A0064540

AttachmentID

AttachmentType

Description EAC FormType

PublicDocument

Trade SecretDocument

Trade SecretJustification

Event Date

694123 EquipmentLeaksFugitivesForm

EAC 3100Processoperation

X

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EPA FORM 3100 – REV2005 1 of 2

FOR OHIO EPA USE FACILITY ID:_____________________________________ EU ID: PTI #:

EMISSIONS ACTIVITY CATEGORY FORM

GENERAL PROCESS OPERATION This form is to be completed for each process operation when there is no specific emissions activity category (EAC) form applicable. If there is more than one end product for this process, copy and complete this form for each additional product (see instructions). Several State/Federal regulations which may apply to process operations are listed in the instructions. Note that there may be other regulations which apply to this emissions unit which are not included in this list. 1. Reason this form is being submitted (Check one) New Permit Renewal or Modification of Air Permit Number(s) (e.g. P001)_______________ 2. Maximum Operating Schedule: 24 hours per day ;365 days per year

If the schedule is less than 24 hours/day or 365 days/year, what limits the schedule to less than maximum? See instructions for examples. NA

3. End product of this process: Fugitive emissions from leaks from Valves and Connectors 4. Hourly production rates (indicate appropriate units). Please see the instructions for clarification of

“Maximum” and “Average” for new versus existing operations:

Hourly Rate Units (e.g., widgets)

Average production

Maximum production 5. Annual production rates (indicate appropriate units) Please see the instructions for clarification of

“Maximum” and “Actual” for new versus existing operations:

Annual Rate Units (e.g., widgets)

Actual production

Maximum production

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EPA FORM 3100 – REV2005 2 of 2

6. Type of operation (please check one):

Continuous Batch (please complete items below)

Minimum cycle* time (minutes): _________ Minimum time between cycles (minutes): _________ Maximum number of cycles per daily 24 hour period: _________

(Note: include cycle time and set up/clean up time.) *”Cycle” refers to the time the equipment is in operation.

7. Materials used in process at maximum hourly production rate (add rows/pages as needed):

Material Physical State at Standard Conditions

Principle Use Amount**

Natural gas gaseous process & combustion

** Please indicate the amount and rate (e.g., lbs/hr, gallons/hr, lbs/cycle, etc.).

8. Please provide a narrative description of the process below (e.g., coating of metal parts using high

VOC content coatings for the manufacture of widgets; emissions controlled by thermal oxidizer...):

See application text for details ___________________________________________________________________________

________________________________________________________________________________

________________________________________________________________________________

________________________________________________________________________________

________________________________________________________________________________

________________________________________________________________________________

________________________________________________________________________________

________________________________________________________________________________

________________________________________________________________________________

________________________________________________________________________________

________________________________________________________________________________

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EPA FORM 3111 - REV2005

FOR OHIO EPA USE FACILITY ID __________________________ EU ID _____________ PTI# _____________

Page 1

EMISSIONS ACTIVITY CATEGORY FORM ROADWAYS AND PARKING AREAS: FUGITIVE DUST EMISSIONS

This form is to be completed for all Roadways and Parking Areas. State/Federal regulations which may apply to Roadways and Parking Areas are listed in the instructions. Note that there may be other regulations which apply to this emissions unit which are not included in this list. 1. Reason this form is being submitted (Check one)

New Permit Renewal or Modification of Air Permit Number(s) (e.g. F001) __F002_____

2. Maximum Operating Schedule: 24_hours per day; 365 days per year

If the schedule is less than 24 hours/day or 365 days/year, what limits the schedule to less than maximum? See instructions for examples. _______________________________

3. Complete the table below for each road segment or parking area. ID

Road Segment or Parking Area

Description

Length

(miles) or Area (ft2)

Year

Installed

Surface

Type (check one)

Surface Composition

(check one)

A

FEL-1

0.01

paved unpaved

asphalt gravel concrete dirt chip & seal other______

B

FEL-2

0.01

paved unpaved

asphalt gravel concrete dirt chip & seal other______

C

FEL-3

0.21

paved unpaved

asphalt gravel concrete dirt chip & seal other______

D

FEL-4

0.2

paved unpaved

asphalt gravel concrete dirt chip & seal other______

E

FEL5

0.1

paved unpaved

asphalt gravel concrete dirt chip & seal other______

F

FEL-6

0.1

paved unpaved

asphalt gravel concrete dirt chip & seal other______

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EPA FORM 3111 - REV2005 Page 2

4. Complete the table below for each paved road segment or parking area.

ID

Silt

Loading (g/m2)

Vehicle Type

Avg.

Weight (tons)

Avg.

Speed (mph)

Vehicle Miles

Traveled (vmt/yr)

Control Method(s)

Application or Usage

Frequency

A

sweeping flushing watering good housekeeping other: __________________

B

sweeping flushing watering good housekeeping other: __________________

C

sweeping flushing watering good housekeeping other: __________________

D

sweeping flushing watering good housekeeping other: __________________

E

sweeping flushing watering good housekeeping other: __________________

F

sweeping flushing watering good housekeeping other: __________________

5. Identify all the places that the permittee=s roadways and parking lots meet a public road. Use the Road Segment or Parking Area ID from the table above to identify the permittee=s roadway and parking lots that are involved. _________________________________ _________________________________

_________________________________ _________________________________ _________________________________ _________________________________

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EPA FORM 3111 - REV2005 Page 3

Describe how any foreign materials deposited on public paved roadways will be removed.

Flushing with water Wet sweeping Sweeping with vacuum truck Other. Describe ________________________________

6. Complete the table below for each unpaved road segment or parking area. ID

Silt

Content (%)

Surface Material Moisture Content

(%)

Vehicle Type

Avg.

Weight (tons)

Avg.

Speed (mph)

Vehicle Miles

Traveled (vmt/yr)

Control Method(s)

Application or

Usage Frequency

A

3.4

Front end loader

66

TBD

5

oiling watering surface improvement chemical stabilization

TBD

B

3.4

Front end loader

66

TBD

278

oiling watering surface improvement chemical stabilization

TBD

C

3.4

Front end loader

66

TBD

3057

oiling watering surface improvement chemical stabilization

TBD

D

3.4

Front end loader

136

TBD

531

oiling watering surface improvement chemical stabilization

TBD

E

3.4

Front end loader

66

TBD

42

oiling watering surface improvement chemical stabilization

TBD

F

3.4

Front end loader

66

TBD

83

oiling watering surface improvement chemical stabilization

TBD

7. The use of used oil for dust suppression is prohibited. Used oil is any oil that has been refined from crude oil, or any synthetic oil, that has

been used, and, as a result of that use, is contaminated by physical or chemical impurities. See OAC rule 3745-279-01. Used oil does not include oils that have been refined from crude oil that have not been used or any synthetic oil that has not been used.

If oiling is being used for dust suppression, is only virgin oil being used?

Yes No Not using oil

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EPA FORM 3111 - REV2005

FOR OHIO EPA USE FACILITY ID __________________________ EU ID _____________ PTI# _____________

Page 1

EMISSIONS ACTIVITY CATEGORY FORM ROADWAYS AND PARKING AREAS: FUGITIVE DUST EMISSIONS

This form is to be completed for all Roadways and Parking Areas. State/Federal regulations which may apply to Roadways and Parking Areas are listed in the instructions. Note that there may be other regulations which apply to this emissions unit which are not included in this list. 1. Reason this form is being submitted (Check one)

New Permit Renewal or Modification of Air Permit Number(s) (e.g. F001) ___F001____

2. Maximum Operating Schedule: 24_hours per day; 365 days per year

If the schedule is less than 24 hours/day or 365 days/year, what limits the schedule to less than maximum? See instructions for examples. _______________________________

3. Complete the table below for each road segment or parking area. ID

Road Segment or Parking Area

Description

Length

(miles) or Area (ft2)

Year

Installed

Surface

Type (check one)

Surface Composition

(check one)

A

HR-1

0.04

paved unpaved

asphalt gravel concrete dirt chip & seal other______

B

HR-2

0.57

paved unpaved

asphalt gravel concrete dirt chip & seal other______

C

HR-3

0.59

paved unpaved

asphalt gravel concrete dirt chip & seal other______

D

HR-4

0.39

paved unpaved

asphalt gravel concrete dirt chip & seal other______

E

HR-5

0.37

paved unpaved

asphalt gravel concrete dirt chip & seal other______

F

paved unpaved

asphalt gravel concrete dirt chip & seal other______

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EPA FORM 3111 - REV2005 Page 2

4. Complete the table below for each paved road segment or parking area.

ID

Silt

Loading (g/m2)

Vehicle Type

Avg.

Weight (tons)

Avg.

Speed (mph)

Vehicle Miles

Traveled (vmt/yr)

Control Method(s)

Application or Usage

Frequency

A

9.7

Trucks

29

TBD

10

sweeping flushing watering good housekeeping other: __________________

TBD

B

9.7

Trucks

29

TBD

8754

sweeping flushing watering good housekeeping other: __________________

TBD

C

9.7

Trucks

29

TBD

377

sweeping flushing watering good housekeeping other: __________________

TBD

D

9.7

Trucks

29

TBD

34427

sweeping flushing watering good housekeeping other: __________________

TBD

E

9.7

Trucks

27

TBD

4321

sweeping flushing watering good housekeeping other: __________________

TBD

F

sweeping flushing watering good housekeeping other: __________________

5. Identify all the places that the permittee=s roadways and parking lots meet a public road. Use the Road Segment or Parking Area ID from the table above to identify the permittee=s roadway and parking lots that are involved. _________________________________ _________________________________

_________________________________ _________________________________ _________________________________ _________________________________

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EPA FORM 3111 - REV2005 Page 3

Describe how any foreign materials deposited on public paved roadways will be removed.

Flushing with water Wet sweeping Sweeping with vacuum truck Other. Describe ________________________________

6. Complete the table below for each unpaved road segment or parking area. ID

Silt

Content (%)

Surface Material Moisture Content

(%)

Vehicle Type

Avg.

Weight (tons)

Avg.

Speed (mph)

Vehicle Miles

Traveled (vmt/yr)

Control Method(s)

Application or

Usage Frequency

A

oiling watering surface improvement chemical stabilization

B

oiling watering surface improvement chemical stabilization

C

oiling watering surface improvement chemical stabilization

D

oiling watering surface improvement chemical stabilization

E

oiling watering surface improvement chemical stabilization

F

oiling watering surface improvement chemical stabilization

7. The use of used oil for dust suppression is prohibited. Used oil is any oil that has been refined from crude oil, or any synthetic oil, that has

been used, and, as a result of that use, is contaminated by physical or chemical impurities. See OAC rule 3745-279-01. Used oil does not include oils that have been refined from crude oil that have not been used or any synthetic oil that has not been used.

If oiling is being used for dust suppression, is only virgin oil being used?

Yes No Not using oil

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EPA Form 3112 – REV 2005 Page 1

EMISSIONS ACTIVITY CATEGORY FORM STORAGE PILES

This form is to be completed for each storage pile. State/Federal regulations which may apply to storage piles are listed in the instructions. Note that there may be other regulations which apply to this emissions unit which are not included in this list.

1. Reason this form is being submitted (Check one)

New Permit Renewal or Modification of Air Permit Number(s) (e.g. F001) _F002_____

2. Maximum Operating Schedule: 24 hours per day; 365 days per year

If the schedule is less than 24 hours/day or 365 days/year, what limits the schedule to less than maximum? See instructions for examples.

3. Meteorological data at or near storage pile area:

a. mean number of days per year in which >0.01 inch of precipitation occurred 120 days b. percentage of time wind speed exceeds 12 miles per hour: 23% c. mean wind speed: 9.4 miles per hour d. source of meteorological data: (a) Toledo airport

(b) AP-42 (c) ________________________________

4. Description of storage pile activities: ID

Type of Material Stored

Method of Load-in

(check one or more)

Method of Load-out (check one or more)

A

HBI

conveyor/stacker: front-end loader other (describe): ________

bucket wheel reclaimer under pile feed rake reclaimer pan scraper front-end loader other: ________

B

conveyor/stacker: front-end loader other (describe): ________

bucket wheel reclaimer under pile feed rake reclaimer pan scraper front-end loader other: ________

C

conveyor/stacker: front-end loader other (describe): ________

bucket wheel reclaimer under pile feed rake reclaimer pan scraper front-end loader other: ________

D

conveyor/stacker: front-end loader other (describe): ________

bucket wheel reclaimer under pile feed rake reclaimer pan scraper front-end loader other: ________

E

conveyor/stacker: front-end loader other (describe): ________

bucket wheel reclaimer under pile feed rake reclaimer pan scraper front-end loader other: ________

FOR OHIO EPA USE FACILITY ID: ______________________ EU ID: __________ PTI#: ___________

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EPA FORM 3112 - REV2005 Page 2

5. STORAGE PILE ACTIVITIES: ID

Number of

Separate Piles

Average Silt

Content (wt %)

Average Moisture

Content (wt %)

Average Pile

Surface Area (acres)

Max. Load-in Rate

(tons/hr)

Max. Load-in Rate

(tons/yr)

Max. Load-out Rate

(tons/hr)

Max. Load-out Rate

(tons/yr)

A

1

1.5

1

4.02

320

2.5 million

800

2.5 million

B

C

D

E

6. WIND EROSION CONTROL METHODS ID

Enclosure, Covering, and/or Operating Practices

(describe)

Chemical

Stabilization (check one or

more)

Application Frequency

Overall Control Eff. (%)

Basis for Overall Wind Erosion Control

Efficiency

A

Chemical stabilization or watering

water crusting agents other:Chemicals

TBD

99

Ohio EPA RACM Guidance

B

water crusting agents other: ________

C

water crusting agents other: ________

D

water crusting agents other: ________

E

water crusting agents other: ________

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EPA FORM 3112 - REV2005 Page 3

7. LOAD-IN CONTROL METHODS ID

Enclosure and/or Operating Practices

(describe)

Chemical

Stabilization

Application Frequency

Overall Control Eff. (%)

Basis for Overall Load-in Control

Efficiency

A

Water or chemical sprays

water dust suppressant other: ________

TBD

84

Ohio EPA RACM Guidance

B

water dust suppressant other: ________

C

water dust suppressant other: ________

D

water dust suppressant other: ________

E

water dust suppressant other: ________

8. LOAD-OUT CONTROL METHODS ID

Enclosure and/or Operating Practices

(describe)

Chemical

Stabilization

Application Frequency

Overall Control Eff. (%)

Basis for Overall Load-out Control

Efficiency

A

Enclosure

water dust suppressant other: ________

B

water dust suppressant other: ________

C

water dust suppressant other: ________

D

water dust suppressant other: ________

E

water dust suppressant

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EPA FORM 3112 - REV2005 Page 4

other: ________

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EPA Form 3112 – REV 2005 Page 1

EMISSIONS ACTIVITY CATEGORY FORM STORAGE PILES

This form is to be completed for each storage pile. State/Federal regulations which may apply to storage piles are listed in the instructions. Note that there may be other regulations which apply to this emissions unit which are not included in this list.

1. Reason this form is being submitted (Check one)

New Permit Renewal or Modification of Air Permit Number(s) (e.g. F001) ____________

2. Maximum Operating Schedule: 24 hours per day; 365 days per year

If the schedule is less than 24 hours/day or 365 days/year, what limits the schedule to less than maximum? See instructions for examples. _______________________________

3. Meteorological data at or near storage pile area:

a. mean number of days per year in which >0.01 inch of precipitation occurred 120 days b. percentage of time wind speed exceeds 12 miles per hour: 23 % c. mean wind speed: 9.4 miles per hour d. source of meteorological data: (a) Toledo airport

(b) AP-42 (c) ________________________________

4. Description of storage pile activities: ID

Type of Material Stored

Method of Load-in

(check one or more)

Method of Load-out (check one or more)

A

Oxide pellets

conveyor/stacker: front-end loader other (describe): ________

bucket wheel reclaimer under pile feed rake reclaimer pan scraper front-end loader other: ________

B

Oxide lumps

conveyor/stacker: front-end loader other (describe): ________

bucket wheel reclaimer under pile feed rake reclaimer pan scraper front-end loader other: ________

C

Oxide fines

conveyor/stacker: front-end loader other (describe): ________

bucket wheel reclaimer under pile feed rake reclaimer pan scraper front-end loader other: ________

D

REMET

conveyor/stacker: front-end loader other (describe): ________

bucket wheel reclaimer under pile feed rake reclaimer pan scraper front-end loader other: ________

E

Feed recovery

conveyor/stacker: front-end loader other (describe): ________

bucket wheel reclaimer under pile feed rake reclaimer pan scraper front-end loader other: ________

FOR OHIO EPA USE FACILITY ID: ______________________ EU ID: __________ PTI#: ___________

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EPA FORM 3112 - REV2005 Page 2

5. STORAGE PILE ACTIVITIES: ID

Number of

Separate Piles

Average Silt

Content (wt %)

Average Moisture

Content (wt %)

Average Pile

Surface Area (acres)

Max. Load-in Rate

(tons/hr)

Max. Load-in Rate

(tons/yr)

Max. Load-out Rate

(tons/hr)

Max. Load-out Rate

(tons/yr)

A

2

3.4

2.5

17.12

3971

3.6 million

1460

3.6 million

B

1

1.7

2.5

0.07

24.3

3595

28

3595

C

1

3.4

1.5

0.27

46

215680

28

215680

D

1

3.4

1.5

0.21

17

107840

29

107840

E

1

3.4

1.5

0.02

0.5

3210

15

3210

6. WIND EROSION CONTROL METHODS ID

Enclosure, Covering, and/or Operating Practices

(describe)

Chemical

Stabilization (check one or

more)

Application Frequency

Overall Control Eff. (%)

Basis for Overall Wind Erosion Control

Efficiency

A

Chemical stabilizatoin/watering

water crusting agents other:Chemicals

TBD

99

Ohio EPA RACM Guidance

B

Chemical stabilizatoin/watering

water crusting agents other: Chemicals

TBD

99

Ohio EPA RACM Guidance

C

Chemical stabilizatoin/watering

water crusting agents other: Chemicals

TBD

99

Ohio EPA RACM Guidance

D

Windshield

water crusting agents other: ________

30

Ohio EPA RACM Guidance

E

Windshield

water crusting agents other: ________

30

Ohio EPA RACM Guidance

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EPA FORM 3112 - REV2005 Page 3

7. LOAD-IN CONTROL METHODS ID

Enclosure and/or Operating Practices

(describe)

Chemical

Stabilization

Application Frequency

Overall Control Eff. (%)

Basis for Overall Load-in Control

Efficiency

A

Water or chemical sprays

water dust suppressant other: ________

TBD

95

Ohio EPA RACM Guidance

B

Water or chemical sprays

water dust suppressant other: ________

TBD

95

Ohio EPA RACM Guidance

C

Water or chemical sprays

water dust suppressant other: ________

TBD

95

Ohio EPA RACM Gudiance

D

Windshield

water dust suppressant other: ________

E

Windshield

water dust suppressant other: ________

8. LOAD-OUT CONTROL METHODS ID

Enclosure and/or Operating Practices

(describe)

Chemical

Stabilization

Application Frequency

Overall Control Eff. (%)

Basis for Overall Load-out Control

Efficiency

A

Water or chemical sprays

water dust suppressant other: ________

TBD

95

Ohio EPA RACM Guidance

B

Enclosure

water dust suppressant other: ________

C

Enclosure

water dust suppressant other: ________

D

Enclosure

water dust suppressant other: ________

E

Enclosure

water dust suppressant

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EPA FORM 3112 - REV2005 Page 4

other: ________

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EPA FORM 3113 - REV2005 Page 1

EMISSIONS ACTIVITY CATEGORY FORM MATERIAL HANDLING: FUGITIVE DUST EMISSIONS

This form is to be completed for any material handling operation with fugitive dust emissions. State/Federal regulations which may apply to material handling operations are listed in the instructions. Note that there may be other regulations which apply to this emissions unit which are not included in this list. 1. Reason this form is being submitted (Check one)

New Permit Renewal or Modification of Air Permit Number(s) (e.g. F001)__F002____

2. Maximum Operating Schedule: 24 hours per day; 365 days per year

If the schedule is less than 24 hours/day or 365 days/year, what limits the schedule to less than maximum? See instructions for examples.

3. What is the material being handled? Hot Briquetted Iron (HBI) 4. Mean wind speed at or near facility 9.4 miles per hour 5. Complete the following table for all unloading operations. ID

Type of Unloading

(see examples below)

Material Unloaded

Annual

Quantity Unloaded (tons/yr)

Hourly

Maximum Unloading

Rate (tons/hr)

Avg. Moisture Content, as

Unloaded (%)

A

Truck: dump pneumatic Vessel: clamshell bucket

ladder Rail car: side dump bottom dump rotary dump pneumatic Other: Conveyor transfer from core plant

HBI

2.48 million

320

1.5

B

Truck: dump pneumatic Vessel: clamshell bucket

ladder Rail car: side dump bottom dump rotary dump pneumatic Other:

C

Truck: dump pneumatic Vessel: clamshell bucket

ladder Rail car: side dump bottom dump rotary dump pneumatic Other: _______________________

FOR OHIO EPA USE FACILITY ID:_____________________ EU ID:__________ PTI#:___________

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EPA FORM 3113 - REV2005 Page 2

D

Truck: dump pneumatic Vessel: clamshell bucket

ladder Rail car: side dump bottom dump rotary dump pneumatic Other: _______________________

6. Complete the following table for all loading operations. ID

Type of Loading

(see examples below)

Material Loaded

Annual

Quantity Loaded (tons/yr)

Hourly

Maximum Loading Rate

(tons/hr)

Avg. Moisture Content, as Loaded (%)

E

front end loader under pile load out bucket well reclaimer rake reclaimer other: __________________

HBI

2.48 million

800

1.5

F

front end loader under pile load out bucket well reclaimer rake reclaimer other: Train loadout

HBI

2.48 million

1213

1.5

G

front end loader under pile load out bucket well reclaimer rake reclaimer other: Truck loadout

HBI

2.19 million

607

1.5

H

front end loader under pile load out bucket well reclaimer rake reclaimer other: __________________

HBI

500000

510

1.5

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EPA FORM 3113 - REV2005 Page 3

7. Complete the following table for all transfer operations.

ID

Type of Transfer Point (see examples below)

Number of Such Points

Type of Material Handled

Max. Transfer Rate (tons/hr)

I

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:_________________________

5

HBI

320 and 800

J

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:_________________________

K

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:_________________________

L

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:_________________________

M

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:_________________________

N

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:_________________________

O

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:_________________________

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EPA FORM 3113 - REV2005 Page 4

8. Summarize the material handling operations covered in items 5 through 7 above and identify the applicable control method(s) from

available options. Complete the remaining table based upon the selected control method(s). ID

Enclosure, Control Equipment

(describe)

Chemical

Stabilization

Application Frequency

Overall Control Eff. (%)

Basis for Overall Control

Efficiency A

See PTI Application

water dust suppressant other: ________

B

water dust suppressant other: ________

C

water dust suppressant other: ________

D

water dust suppressant other: ________

E

water dust suppressant other: ________

F

water dust suppressant other: ________

G

water dust suppressant other: ________

H

water dust suppressant other: ________

I

water dust suppressant other: ________

J

water dust suppressant other: ________

K

water dust suppressant other: ________

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EPA FORM 3113 - REV2005 Page 5

L

water dust suppressant other: ________

M

water dust suppressant other: ________

N

water dust suppressant other: ________

O

water dust suppressant other: ________

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EPA FORM 3113 - REV2005 Page 1

EMISSIONS ACTIVITY CATEGORY FORM MATERIAL HANDLING: FUGITIVE DUST EMISSIONS

This form is to be completed for any material handling operation with fugitive dust emissions. State/Federal regulations which may apply to material handling operations are listed in the instructions. Note that there may be other regulations which apply to this emissions unit which are not included in this list. 1. Reason this form is being submitted (Check one)

New Permit Renewal or Modification of Air Permit Number(s) (e.g. F001)__F002____

2. Maximum Operating Schedule: 24 hours per day; 365 days per year

If the schedule is less than 24 hours/day or 365 days/year, what limits the schedule to less than maximum? See instructions for examples.

3. What is the material being handled? Iron oxide pellets 4. Mean wind speed at or near facility 9.4 miles per hour 5. Complete the following table for all unloading operations. ID

Type of Unloading

(see examples below)

Material Unloaded

Annual

Quantity Unloaded (tons/yr)

Hourly

Maximum Unloading

Rate (tons/hr)

Avg. Moisture Content, as

Unloaded (%)

A

Truck: dump pneumatic Vessel: clamshell bucket

ladder Rail car: side dump bottom dump rotary dump pneumatic Other: Conveyor transfer from Midwest

Oxide pellets

3.6 Million

3,970 and 1,460

2.5

B

Truck: dump pneumatic Vessel: clamshell bucket

ladder Rail car: side dump bottom dump rotary dump pneumatic Other: Drop from conveyor

Oxide lumps

3,595

24.3

2.5

C

Truck: dump pneumatic Vessel: clamshell bucket

ladder Rail car: side dump bottom dump rotary dump pneumatic Other: Drop from conveyor

Oxide fines

215,680

46.3

1.5

FOR OHIO EPA USE FACILITY ID:_____________________ EU ID:__________ PTI#:___________

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EPA FORM 3113 - REV2005 Page 2

D

Truck: dump pneumatic Vessel: clamshell bucket

ladder Rail car: side dump bottom dump rotary dump pneumatic Other: Drop from conveyor

REMET

107,840

17

1.5

6. Complete the following table for all loading operations. ID

Type of Loading

(see examples below)

Material Loaded

Annual

Quantity Loaded (tons/yr)

Hourly

Maximum Loading Rate

(tons/hr)

Avg. Moisture Content, as Loaded (%)

E

front end loader under pile load out bucket well reclaimer rake reclaimer other: __________________

Oxide pellets

3.6 Million

3,970

2.5

F

front end loader under pile load out bucket well reclaimer rake reclaimer other: __________________

Oxide lumps

3,595

28

2.5

G

front end loader under pile load out bucket well reclaimer rake reclaimer other: __________________

Oxide fines

71,893

28

1.5

H

front end loader under pile load out bucket well reclaimer rake reclaimer other: __________________

REMET

107,840

29

1.5

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EPA FORM 3113 - REV2005 Page 3

7. Complete the following table for all transfer operations.

ID

Type of Transfer Point (see examples below)

Number of Such Points

Type of Material Handled

Max. Transfer Rate (tons/hr)

I

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:_________________________

1

Oxide pellets

3,970

J

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:_________________________

1

Oxide lumps

24.3

K

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:_________________________

1

Oxide fines

46.3

L

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:_________________________

1

REMET

14

M

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:_________________________

5

Oxide

3,970 and 1,460

N

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:day bins and conveyors

2

Oxide

560

O

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:screen and conveyors and coating

3

Oxide screen transfers and coating handling

560

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EPA FORM 3113 - REV2005 Page 4

8. Summarize the material handling operations covered in items 5 through 7 above and identify the applicable control method(s) from

available options. Complete the remaining table based upon the selected control method(s). ID

Enclosure, Control Equipment

(describe)

Chemical

Stabilization

Application Frequency

Overall Control Eff. (%)

Basis for Overall Control

Efficiency A

See PTI Application

water dust suppressant other: ________

B

water dust suppressant other: ________

C

water dust suppressant other: ________

D

water dust suppressant other: ________

E

water dust suppressant other: ________

F

water dust suppressant other: ________

G

water dust suppressant other: ________

H

water dust suppressant other: ________

I

water dust suppressant other: ________

J

water dust suppressant other: ________

K

water dust suppressant other: ________

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EPA FORM 3113 - REV2005 Page 5

L

water dust suppressant other: ________

M

water dust suppressant other: ________

N

water dust suppressant other: ________

O

water dust suppressant other: ________

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EPA FORM 3113 - REV2005 Page 1

EMISSIONS ACTIVITY CATEGORY FORM MATERIAL HANDLING: FUGITIVE DUST EMISSIONS

This form is to be completed for any material handling operation with fugitive dust emissions. State/Federal regulations which may apply to material handling operations are listed in the instructions. Note that there may be other regulations which apply to this emissions unit which are not included in this list. 1. Reason this form is being submitted (Check one)

New Permit Renewal or Modification of Air Permit Number(s) (e.g. F001)__F002____

2. Maximum Operating Schedule: 24 hours per day; 365 days per year

If the schedule is less than 24 hours/day or 365 days/year, what limits the schedule to less than maximum? See instructions for examples.

3. What is the material being handled? Iron oxide pellets 4. Mean wind speed at or near facility 9.4 miles per hour 5. Complete the following table for all unloading operations. ID

Type of Unloading

(see examples below)

Material Unloaded

Annual

Quantity Unloaded (tons/yr)

Hourly

Maximum Unloading

Rate (tons/hr)

Avg. Moisture Content, as

Unloaded (%)

A

Truck: dump pneumatic Vessel: clamshell bucket

ladder Rail car: side dump bottom dump rotary dump pneumatic Other: Conveyor transfer from Midwest

Feed Recovery

3210

0.5

1.5

B

Truck: dump pneumatic Vessel: clamshell bucket

ladder Rail car: side dump bottom dump rotary dump pneumatic Other: Drop from conveyor

C

Truck: dump pneumatic Vessel: clamshell bucket

ladder Rail car: side dump bottom dump rotary dump pneumatic Other: Drop from conveyor

FOR OHIO EPA USE FACILITY ID:_____________________ EU ID:__________ PTI#:___________

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EPA FORM 3113 - REV2005 Page 2

D

Truck: dump pneumatic Vessel: clamshell bucket

ladder Rail car: side dump bottom dump rotary dump pneumatic Other: Drop from conveyor

6. Complete the following table for all loading operations. ID

Type of Loading

(see examples below)

Material Loaded

Annual

Quantity Loaded (tons/yr)

Hourly

Maximum Loading Rate

(tons/hr)

Avg. Moisture Content, as Loaded (%)

E

front end loader under pile load out bucket well reclaimer rake reclaimer other: __________________

Feed recovery

3210

0.5

1.5

F

front end loader under pile load out bucket well reclaimer rake reclaimer other: __________________

G

front end loader under pile load out bucket well reclaimer rake reclaimer other: __________________

H

front end loader under pile load out bucket well reclaimer rake reclaimer other: __________________

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EPA FORM 3113 - REV2005 Page 3

7. Complete the following table for all transfer operations.

ID

Type of Transfer Point (see examples below)

Number of Such Points

Type of Material Handled

Max. Transfer Rate (tons/hr)

I

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:_________________________

1

Feed recovery

0.5

J

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:_________________________

K

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:_________________________

L

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:_________________________

M

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:_________________________

N

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:day bins and conveyors

O

Load/unload conveyor: vibrating belt screw bucket elevator belt conveyor to belt conveyor

Other:screen and conveyors and coating

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EPA FORM 3113 - REV2005 Page 4

8. Summarize the material handling operations covered in items 5 through 7 above and identify the applicable control method(s) from

available options. Complete the remaining table based upon the selected control method(s). ID

Enclosure, Control Equipment

(describe)

Chemical

Stabilization

Application Frequency

Overall Control Eff. (%)

Basis for Overall Control

Efficiency A

See PTI Application

water dust suppressant other: ________

B

water dust suppressant other: ________

C

water dust suppressant other: ________

D

water dust suppressant other: ________

E

water dust suppressant other: ________

F

water dust suppressant other: ________

G

water dust suppressant other: ________

H

water dust suppressant other: ________

I

water dust suppressant other: ________

J

water dust suppressant other: ________

K

water dust suppressant other: ________

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EPA FORM 3113 - REV2005 Page 5

L

water dust suppressant other: ________

M

water dust suppressant other: ________

N

water dust suppressant other: ________

O

water dust suppressant other: ________

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EMISSIONS ACTIVITY CATEGORY FORM INTERNAL COMBUSTION ENGINES OR TURBINES

This form is to be completed for each reciprocating engines or turbines. State/Federal regulations which may apply to internal combustion engines are listed in the instructions. Note that there may be other regulations which apply to this emissions unit which are not included in this list.

1. Maximum Operating Schedule: _________ hours per day; ________ days per year

If the schedule is less than 24 hours/day or 365 days/year, what limits the schedule to less than maximum? See instructions for examples. Less than 500 hours/year

2. Engine type: Turbine Reciprocating

3. Purpose of engine: Driving pump or compressor Driving electrical generator

4. Normal use of engine: Emergency only Non-emergency

5. Engine Manufacturer: TBD Model No: TBD

Model Year: TBD Serial Number: TBD

Date engine was ordered from the manufacturer: ____TBD_________________________

Date engine was first installed at any location by any operator/facility: TBD

Has the manufacturer certified the engine to meet any emissions standards? No Yes

If yes, which Part and paragraph and/or Table and/or Tier has been met? NSPS IIII

Will the engine be operated under the conditions the manufacturer has identified as necessary to meet these standards? No Yes

6. Type of ignition: compression (diesel) spark

7. Displacement (for reciprocating engines only): ____1.5_ (Liters/cylinder, for compression ignition)

________________________(cubic centimeters, for spark ignition)

8. Engine exhaust configuration (for turbines only): simple cycle (no heat recovery) regenerative cycle (heat recovery to preheat combustion air) cogeneration cycle (heat recovered to produce steam) combined cycle (heat recovered to produce steam which drives generator)

FOR OHIO EPA USE FACILITY ID: _________________ EU ID: _______ Application #:__________

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9. Input capacities (million BTU/hr): Rated: 2.42 Maximum 2.42 Normal 2.42

Supplemental burner (duct burner) input capacity, if equipped (million BTU/hr):

Rated:_________ Maximum ___________ Normal ___________

10. Output capacities (Horsepower): Rated: 311 Maximum 311 Normal 311

(Kilowatts): Rated: _________ Maximum ___________ Normal ___________

(lbs steam/hr)*: Rated: _________ Maximum ___________ Normal ___________ *(for cogeneration or combined cycle units only)

11. Type of fuel fired (check all that apply): single fuel No. 2 oil, low-sulfur natural gas landfill gas dual fuel No. 2 oil, high-sulfur diesel digester gas gasoline propane other, explain

12. Complete the following table for all fuels identified in question 11 that are used for the engine and any supplemental (duct) burners, if equipped:

Fuel Heat Content

(BTU/unit) wt.% Ash

wt.% Sulfur

Fuel Usage

Estimated Maximum Per Year Normal Per Hour Max. Per Hour

Nat. gas

BTU/cu ft

gr/scf

cu ft

cu ft

cu ft

No. 2 oil

BTU/gal

gal

gal

gal

Gasoline

BTU/gal

gal

gal

gal

Diesel

137,452 BTU/gal

0.0015

7000 gal

gal

gal

Landfill/digester gas

BTU/cu ft

ppm

cu ft

cu ft

cu ft

Other (show units)

List supplemental (duct) burner fuel and information below (show units):

13. Type of combustion cycle (check all that apply):

2-stroke 4-stroke carbureted rich-burn lean-burn fuel injected other, explain ________________________________________________

14. Emissions control techniques (check all that apply): prestratified charge nonselective catalytic reduction (NSCR) water/steam injection air/fuel ratio selective catalytic reduction (SCR) injection timing retard catalytic oxidation 2-stage rich/lean combustion 2-stage lean/lean combustion preignition chamber combustion (PCC) diesel particulate filter other, explain________________________

For each emissions control technique checked above, explain what pollutants are controlled by each technique: _ ____________________________________________________________________________ ____________________________________________________________________________

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15. Has the engine been modified or reconstructed since its manufacture date: No Yes If Yes, explain: ______________________________________________________________________________

______________________________________________________________________________ ______________________________________________________________________________

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EMISSIONS ACTIVITY CATEGORY FORM INTERNAL COMBUSTION ENGINES OR TURBINES

This form is to be completed for each reciprocating engines or turbines. State/Federal regulations which may apply to internal combustion engines are listed in the instructions. Note that there may be other regulations which apply to this emissions unit which are not included in this list.

1. Maximum Operating Schedule: _________ hours per day; ________ days per year

If the schedule is less than 24 hours/day or 365 days/year, what limits the schedule to less than maximum? See instructions for examples. Less than 500 hours/year

2. Engine type: Turbine Reciprocating

3. Purpose of engine: Driving pump or compressor Driving electrical generator

4. Normal use of engine: Emergency only Non-emergency

5. Engine Manufacturer: TBD Model No: TBD

Model Year: TBD Serial Number: TBD

Date engine was ordered from the manufacturer: ____TBD_________________________

Date engine was first installed at any location by any operator/facility: TBD

Has the manufacturer certified the engine to meet any emissions standards? No Yes

If yes, which Part and paragraph and/or Table and/or Tier has been met? NSPS IIII

Will the engine be operated under the conditions the manufacturer has identified as necessary to meet these standards? No Yes

6. Type of ignition: compression (diesel) spark

7. Displacement (for reciprocating engines only): _________1.12____(Liters/cylinder, for compression ignition)

________________________(cubic centimeters, for spark ignition)

8. Engine exhaust configuration (for turbines only): simple cycle (no heat recovery) regenerative cycle (heat recovery to preheat combustion air) cogeneration cycle (heat recovered to produce steam) combined cycle (heat recovered to produce steam which drives generator)

FOR OHIO EPA USE FACILITY ID: _________________ EU ID: _______ Application #:__________

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9. Input capacities (million BTU/hr): Rated: 0.95 Maximum 0.95 Normal 0.95

Supplemental burner (duct burner) input capacity, if equipped (million BTU/hr):

Rated:_________ Maximum ___________ Normal ___________

10. Output capacities (Horsepower): Rated: 133 Maximum 133 Normal 133

(Kilowatts): Rated: _________ Maximum ___________ Normal ___________

(lbs steam/hr)*: Rated: _________ Maximum ___________ Normal ___________ *(for cogeneration or combined cycle units only)

11. Type of fuel fired (check all that apply): single fuel No. 2 oil, low-sulfur natural gas landfill gas dual fuel No. 2 oil, high-sulfur diesel digester gas gasoline propane other, explain

12. Complete the following table for all fuels identified in question 11 that are used for the engine and any supplemental (duct) burners, if equipped:

Fuel Heat Content

(BTU/unit) wt.% Ash

wt.% Sulfur

Fuel Usage

Estimated Maximum Per Year Normal Per Hour Max. Per Hour

Nat. gas

BTU/cu ft

gr/scf

cu ft

cu ft

cu ft

No. 2 oil

BTU/gal

gal

gal

gal

Gasoline

BTU/gal

gal

gal

gal

Diesel

137,452 BTU/gal

0.0015

60,500 gal

gal

gal

Landfill/digester gas

BTU/cu ft

ppm

cu ft

cu ft

cu ft

Other (show units)

List supplemental (duct) burner fuel and information below (show units):

13. Type of combustion cycle (check all that apply):

2-stroke 4-stroke carbureted rich-burn lean-burn fuel injected other, explain ________________________________________________

14. Emissions control techniques (check all that apply): prestratified charge nonselective catalytic reduction (NSCR) water/steam injection air/fuel ratio selective catalytic reduction (SCR) injection timing retard catalytic oxidation 2-stage rich/lean combustion 2-stage lean/lean combustion preignition chamber combustion (PCC) diesel particulate filter other, explain________________________

For each emissions control technique checked above, explain what pollutants are controlled by each technique: _ ____________________________________________________________________________ ____________________________________________________________________________

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15. Has the engine been modified or reconstructed since its manufacture date: No Yes If Yes, explain: ______________________________________________________________________________

______________________________________________________________________________ ______________________________________________________________________________

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Appendix B – Emissions Calculations

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IronUnits LLC

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Cliffs HBI Project (Mudhen) - Inputs MIDREX ProcessRevised Calculations Post Permit IssuanceParameter Value UnitsOxide Rate from Dock 3970 tons/hour to the plantOxide Rate to Day Bin 1460 tons/hourOxide Rate to Screen and Core Plant 560 tons/hourOxide Rate to Core Plant 3,594,666 tons/yearOxide Lumps Rate to Pile 24.3 tons/hourOxide Lumps Rate to Pile 3,595 tons/yearOxide Fines Rate to Pile 46.3 tons/hourOxide Fines Rate to Pile 215,680 tons/yearPortland Cement Coating 8,987 tons/yearREMET Rate to Pile 17 tons/hourREMET Rate to Pile 107,840 tons/yearWastewater Treatment Sludge 142,040 tons/year

Oxide stockpile 772,000 tonsOxide Lumps stockpile 1,200 tonsOxide Fines stockpile 5,600 tonsREMET stockpile 6,700 tons

HBI Throughput 316 tons/hourHBI Throughput 2,479,080 tons/yearHBI Annual Reclaim by FEL 20%Trucking Annual Proportion 55%Truck operation hours 4,380 hour/year 12 hour shift & 7 days/weekOperation 8,760 hour/yearHBI Stockpile 111,000 tonsNote: All tons per hour rates represent at least 24-hour or longer average rates.

NG rates and conversion1 Nm3 = 37.93 scf 0.0387 MMBtu

LHV HHVNG 950 1020 ratio 1.073684211Per MIDREX Heat Input 6/15/2017 email attachment

Reformer Heat Input 1687 MMBtu/hour (HHV)@ 4.2% carbon using ACTFraction of virgin NG 20%Reformer NG HI 337.4 MMBtu/hour (HHV)

CO2 (1) CH4 (2) N2O (3)Natural Gas (kg/MMBtu) 53.06 0.001 0.0001GWP 1 25 298Natural Gas CO2e= 117.10 lb/MMBtu

Notes: 1. 40 CFR 98, Table C-1 (revised 11/29/13).2. 40 CFR 98, Table C-2 (revised 11/29/13).3. 40 CFR 98, Table A-1 (revised 11/29/13).

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IronUnits LLC

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Summary of Potential to Emit

Emissions (tons/year)Sheet Ref EU ID Emission Unit PM PM10 PM2.5 NOx SO2 CO VOC CO2 CO2e Total HAPs Hexane Formaldehyde Chloroform NH3C-1a MTR-5 Midwest Hopper to Conveyor 0.04 0.04 0.04C-1b TR-1 Conveyor to Transfer Tower-I 0.08 0.08 0.08C-2 TR-2 Conveyor to Stacker Machine 0.38 0.18 0.03C-3 WE-1 Oxide Stockpile Wind Erosion 0.19 0.10 0.04C-4 TR-3 Stacker to Stockpile 0.35 0.17 0.03C-5 TR-4 Bucket Reclaim to Conveyor to Main Conveyor 0.35 0.17 0.03C-6 TR-5 Reclaim Conveyor to Conveyor 0.38 0.18 0.03C-7 TR-6, 7 Conveyor Transfer in Transfer Tower II & III 0.44 0.44 0.44C-8 TR-8 Oxide Lumps to Stockpile 0.0004 0.0002 0.00003C-9 WE-2 Oxide Lumps Stockpile Wind Erosion 0.0004 0.0002 0.0001C-10 FEL-1 FEL Fugitives for Oxide Lumps 0.0007 0.0002 0.00002C-11 TR-9 Oxide Lumps Transfer from FEL to Truck 0.0071 0.0033 0.00051C-12 HR-1 Oxides Lumps Truck Transport Fugitives 0.0006 0.0001 0.00003C-13 TR-10 Oxide Bins Drops 1.57 1.57 1.57C-14 TR-11 Oxide Fines to Stockpile 0.04 0.021 0.003C-15 WE-3 Oxide Fines Stockpile Wind Erosion 0.003 0.002 0.0006C-16 FEL-2 FEL Oxides Fine Reclaim Fugitives 0.04 0.009 0.0009C-17 TR-12 Oxide Fines from FEL to Truck 0.87 0.411 0.062C-18 HR-2 Truck for Oxide Fines transport fugitives 0.49 0.10 0.02C-19 SR-1 Screen Building Baghouse Exhaust 1.10 1.10 1.10C-20a TR-13a Oxide Transfer from Conveyor to Bucket Elevator 0.29 0.29 0.29C-20b TR-13b Conveyors with Fines Transfer Tower 0.35 0.35 0.35C-21 TR-14 Coating Storage and Mixing and Fines Transfer Tower 0.08 0.08 0.08C-22 HR-3 Coating Transport Trucks 0.02 0.005 0.001C-23 TR-15 REMET Drop to Stockpile 0.43 0.21 0.031C-24 WE-4 REMET Stockpile Wind Erosion 0.17 0.08 0.03C-25 FEL-3 REMET Reclaim FEL fugitives 0.42 0.10 0.01C-26 TR-16 REMET Transfer from FEL to Hopper 0.43 0.21 0.03C-27 TR-17, TR-18 Two HBI Conveyor Transfer Towers 0.67 0.67 0.67C-28 TR-19 HBI Conveyor to Stacker Machine 0.54 0.09 0.038C-29 TR-20 HBI Transfer from Stacker Conveyor to Stockpile 0.88 0.14 0.06C-30 WE-5 HBI Stockpile Wind Erosion 0.02 0.01 0.004C-31 FEL-4 HBI Reclaim FEL fugitives 0.10 0.02 0.00C-32a TR-21a HBI Reclaim Bucket Wheel to Conveyor 0.50 0.08 0.03C-32b TR-21b HBI Reclaim Conveyor to Enclosed Conveyor 0.54 0.09 0.04C-32c TR-21c HBI Drop from FEL to Hopper 0.10 0.02 0.01C-33 TR-22 HBI Drop from Hopper to Conveyor 0.11 0.02 0.01C-34 TR-23 HBI Conveyor Transfer Tower to Loadout 0.18 0.18 0.18C-35 TR-24 HBI Conveyor to loading bin for train and truck loadout 0.15 0.15 0.15C-36 TR-25 HBI Truck Loadout Scrubber 0.46 0.46 0.46C-37a TR-26 HBI Drop from Loadout to Train 0.03 0.00 0.00C-37b TR-27 HBI Drop from Loadout to Truck 0.02 0.00 0.00C-38 HR-4 HBI Truck transport fugitives 3.46 0.69 0.17C-39a TR-28a Furnace Feed Conveyor Exhaust 0.24 0.24 0.24C-39b TR-28b Furnace Charge Hopper Exhaust 0.44 0.44 0.44 8.85 1.05 12.36 5,891 5,891C-40 P-1 Bottom Seal Gas Exhaust 11.21 11.44 11.44 1.88 1.05 4,318.80 3,666 3,666C-41 P-2 Reformer Exhaust 35.30 81.96 81.96 436.89 22.12 229.29 7.97 1,553,868 1,554,047 2.74 2.61 0.11C-42 P-3 Hot Briquette Exhaust 17.39 17.96 17.96 17.25 0.92 3,994.62 54,071 54,071C-43 P-4 Briquette Cooling System Vapor Removal Vent 14.47 14.47 14.47 2,602.05C-44 P-5 Degasser Exhaust 482.05 18,054 18,054 17.39C-45a P-6a Flare (SD/SU/Upsets) 0.16 0.64 0.64 5.83 0.05 26.58 4.44 10,031 10,042C-45b P-6b Flare (Pilot Only) 0.01 0.02 0.02 0.22 0.002 0.98 0.16 371 371 0.01 0.01 0.00C-46 P-7 Cooling Tower 0.30 0.09 0.06 0.12 0.12 0.12 9.86C-47 P-8 Emergency Fire Water Booster 0.03 0.03 0.03 0.51 0.001 0.45 0.20 98 99 1.34E-03C-48 P-9 Emergency Generator 0.22 0.25 0.25 7.05 0.01 3.86 0.43 681 683C-49 FugGHG Fugitive Emissions from Components 3.06 2757C-53 TR-29 Feed Recovery Transfer to Stockpile 0.01 0.01 0.00C-54 WE-6 Feed Recovery Stockpile Wind Erosion 0.02 0.01 0.00C-55 FEL-5 Feed Recovery FEL Fugitives 0.01 0.00 0.00C-56 TR-30 Feed Recovery FEL to Hopper 0.01 0.01 0.00C-57 FEL-6 Product Oversize FEL Fugitives 0.01 0.00 0.00C-58 TR-31 Product Oversize FEL to Hopper 0.03 0.01 0.00C-59 P-10 Admin Building Generator 0.02 0.02 0.02 0.22 0.00 0.27 0.02 38.81 38.95C-60 HR-5 Sludge Truck Transport Fugitives 0.23 0.05 0.01

Total 96.41 136.16 133.68 478.70 25.20 11,671.32 16.40 1,646,771 1,649,721 2.87 2.61 0.11 0.12 27.24Core Plant Revised rates

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Midwest Terminals of Toledo, Inc.

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Table C-1a: Midwest Hopper to Conveyor (Controlled)

Emission Unit: MTR-5 Oxide Midwest Hopper to Conveyor to Transfer Tower to Conveyor with BaghouseCH2M GAD Points 17

Parameters:Oxide rate to Cliffs 3,970 tons/hourExpected operation 1,200 hours/year Based on 80% hourly operating rateDesign exhaust volume 3,055 dscfmMaximum exhaust rate scaleup 110%Design PM grain loading 0.0025 gr/dscf BACT limit from Essar MN Permit

Potential to Emit:Pollutant Controlled

Conveyor Transfers (lb/hour)

Emissions (tons/year)

PM 0.07 0.04PM10 0.07 0.04PM2.5 0.07 0.04Assuming PM10 and PM2.5 equals PMScaled up design flow was used here

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IronUnits LLC

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Table C-1b: Conveyor from Midwest Terminal to Conveyor in Transfer Tower-I (Controlled)

Emission Unit: TR-1, Oxide Midwest Conveyor to Stacker Transfer Tower-I with BaghouseCH2M GAD Points 18

Parameters:Oxide rate to Cliffs 3970 tons/hourExpected operation 1,200 hours/year Based on 80% hourly operating rateDesign exhaust volume 6,110 dscfmMaximum exhaust rate scaleup 110%Design PM grain loading 0.0025 gr/dscf BACT limit from Essar MN Permit

Potential to Emit:Pollutant Controlled

Transfer Tower (lb/hour)

Emissions (tons/year)

PM 0.13 0.08PM10 0.13 0.08PM2.5 0.13 0.08Assuming PM10 and PM2.5 equals PMScaled up design flow was used here

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IronUnits LLC

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Table C-2: Conveyor from Transfer Tower to Stacker Machine Conveyor (Windshield)

Emission Unit: TR-2, Conveyor to Stacker Machine Conveyor with WindshieldCH2M GAD Point 20

Parameters:Oxide transfer rate from boat 3,970 tons/hour

3,594,666 tons/yearExpected operation 1,200 hours/year Same as transfer towerNumber of drop points with water spray for stacking 1U = mean windspeed 1 mph Windshield around the transfer to reduce wind effectM = moisture content 2.5 %

Oxide drop point (open) emission factorsPM 0.0002 lb/tonPM10 0.0001 lb/tonPM2.5 0.00002 lb/tonAP-42, Page 13.2.4-3 (11/2006)

Potential to Emit:Pollutant Transfer from

Conveyor to Stacker (lb/hour)

Total Emissions (tons/year)

PM 0.85 0.38PM10 0.40 0.18PM2.5 0.06 0.03

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IronUnits LLC

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Table C-3: Oxide Stockpile Wind Erosion (Water or Chemical stabilization)

Emission Unit: WE-1, Wind Erosion from Oxide StockpilesCH2M GAD Point 19

Parameters:Iron oxide stockpile 772,000 tonsVoid ratio 0.1 assumed 10% voidIron oxide density 130 lb/cfVolume of pile Vp 13,196,581 cfAngle of repose 26 degrees From engineering estimateNumber of stockpiles 2Width of stockpile 148 feetHeight of stockpile 36 feet Using angle of repose and pile widthVolume of conical part of stockpile 205,326 cf =pi*(d/2)^2*h/3Remaining volume in triangle section 6,392,965 cf Calculated for one pileLength of triangle section of stockpile 2410 feet Volume of prism = 1/2*a*c*hStockpile Area 17.12 acres Area for 2 pilesAnnual stockpile days 365 days/yearIron oxide silt content 3.4 wt. % AP-42; Table 13.2.4-1, Taconite Mining and Processing (Pellets); 11/06Threshold wind speed 23 % of time % of time that wind speed exceeds 12 mph at 10 m for Toledo airport dataDays with >0.01" precipitation 120 days/yr AP-42; Figure 13.2.1-2; 1/11 for Toledo, OhioCont. eff. using water or chemical stabilization 99% Ohio EPA RACM Guidance Table 2.1.2-8

Stockpile wind erosion uncontrolled emission factorsPM 6.2 lb/day/acrePM10 3.1 lb/day/acrePM2.5 1.2 lb/day/acreAir Pollution Engineering Manual; p 136; Eqn. 5; AWMA; 1992

Potential to Emit:Pollutant Controlled

Stockpile Emissions (lb/hour)*

Emissions (tons/year)

PM 0.09 0.19PM10 0.04 0.10PM2.5 0.02 0.04*Max hourly calculated by doubling the hourly rate

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IronUnits LLC

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Table C-4: Stacker Machine Conveyor to Pile (Water or chemical sprays)

Emission Unit: TR-3, Stacker Conveyor to Stockpile using Sprays with ChemicalsCH2M GAD Points 21

Parameters:Oxide transfer rate from boat 3,970 tons/hour

3,594,666 tons/yearExpected operation 1,200 hours/year Assuming same as transfer to Stacker machineNumber of controlled drop points 1U = mean windspeed for Toledo 9.40 mph AP-42, Table 7.1-9, 11/2006M = moisture content 2.5 %Water or chemical sprays control eff. 95% Ohio EPA RACM Guidance Table 2.1.3-3

Oxide drop point (open) emission factorsPM 0.004 lb/tonPM10 0.002 lb/tonPM2.5 0.0003 lb/tonAP-42, Page 13.2.4-3 (11/2006)

Potential to Emit:Pollutant Controlled

Stacking Stockpile (lb/hour)

Total Emissions (tons/year)

PM 0.78 0.35PM10 0.37 0.17PM2.5 0.06 0.03

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IronUnits LLC

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Table C-5: Bucket Wheel Reclaim to Conveyor (Water or chemical sprays)

Emission Unit: TR-4, Reclaim using Bucket Wheel to Conveyor using Sprays with ChemicalsCH2M GAD Point 22

Parameters:Oxide transfer rate from reclaim 1,460 tons/hour

3,594,666 tons/yearExpected operation 3,078 hours/year Assuming 80% hourly operating rateNumber of controlled drop points 1U = mean windspeed for Toledo 9.40 mph AP-42, Table 7.1-9, 11/2006M = moisture content 2.5 %Water or chemical sprays control eff. 95% Ohio EPA RACM Guidance Table 2.1.3-3

Oxide drop point (open) emission factorsPM 0.004 lb/tonPM10 0.002 lb/tonPM2.5 0.0003 lb/tonAP-42, Page 13.2.4-3 (11/2006)

Potential to Emit:Pollutant Controlled

Transfer from Reclaim Bucket to Conveyor (lb/hour)

Total Emissions (tons/year)

PM 0.29 0.35PM10 0.14 0.17PM2.5 0.02 0.03

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IronUnits LLC

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Table C-6: Conveyor from Reclaim Machine to Main Conveyor (Windshield)

Emission Unit: TR-5, Oxide Conveyor from Reclaim Machine to Conveyor with WindshieldCH2M GAD Points 23

Parameters:Oxide transfer rate from reclaim 1,460 tons/hour

3,594,666 tons/yearExpected operation 3,078 hours/year Same as ReclaimNumber of controlled drop points 1U = mean windspeed 1 mph Windshield around the transfer to reduce wind effectM = moisture content 2.5 %

Oxide drop point (open) emission factorsPM 0.0002 lb/tonPM10 0.0001 lb/tonPM2.5 0.00002 lb/tonAP-42, Page 13.2.4-3 (11/2006)

Potential to Emit:Pollutant Transfer from

Reclaim to Conveyor (lb/hour)

Total Emissions (tons/year)

PM 0.31 0.38PM10 0.15 0.18PM2.5 0.02 0.03No control efficiency is applied

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IronUnits LLC

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Table C-7: Conveyor from Reclaim to Conveyor in Transfer Tower-II and III (Controlled)

Emission Unit: TR-6, TR-7 Oxide Conveyor from Reclaim to Conveyor Transfer Tower-II and III with BaghousesCH2M GAD Points 24 & 25

Parameters:Oxide rate from reclaim 1460 tons/hourExpected operation 5,000 hours/year Twice the annual througput rate divided by hourly rateDesign exhaust volume 4,073 dscfmMaximum exhaust rate scaleup 110%Design PM grain loading 0.0025 gr/dscf BACT limit from Essar MN Permit

Potential to Emit:Pollutant Controlled

Transfer Tower TR-6 (lb/hour)

Controlled Transfer Tower TR-7 (lb/hour)

Emissions (tons/year)

PM 0.09 0.09 0.44PM10 0.09 0.09 0.44PM2.5 0.09 0.09 0.44Assuming PM10 and PM2.5 equals PMScaled up design flow was used here

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IronUnits LLC

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Table C-8: Oxide Lumps Conveyor Drop (Water or chemical sprays)

Emission Unit: TR-8 Oxide Lumps from Conveyor to StockpileCH2M GAD Points 27

Parameters:Oxide lumps transfer rate 24.3 tons/hour

3,595 tons/yearExpected operation 185 hours/year Assuming 80% hourly operating rateNumber of drop points 1U = mean windspeed for Toledo 9.40 mph AP-42, Table 7.1-9, 11/2006M = moisture content 2.5 % Assumes same as oxide pelletsWater or chemical sprays control eff. 95% Ohio EPA RACM Guidance Table 2.1.3-3

Oxide lumps drop point uncontrolled emission factorsPM 0.004 lb/tonPM10 0.002 lb/tonPM2.5 0.0003 lb/tonAP-42, Page 13.2.4-3 (11/2006)

Potential to Emit:Pollutant Controlled Oxide

Lumps Drop (lb/hour)

Total Emissions (tons/year)

PM 0.005 0.00PM10 0.002 0.00PM2.5 0.000 0.00

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IronUnits LLC

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Table C-9: Oxide Lumps Stockpile Wind Erosion (Water or Chemical stabilization)

Emission Unit: WE-2, Wind Erosion from Oxide Lumps StockpilesCH2M GAD Points 28

Parameters:Oxide Lumps stockpile 1,200 tonsVoid ratio 0.1 assumed 10% voidDensity 143 lb/cf 10% higher than the iron oxidesVolume of pile Vp 18,648 cfAngle of repose 35 degrees http://www.ckit.co.za/secure/misc/trajectories_material.htmlNumber of stockpiles 1Diameter of stockpile 59 feetHeight of stockpile 21 feet Using angle of repose and pile widthVolume of conical part of stockpile 19,018 cf =pi*(d/2)^2*h/3Stockpile Area 0.07 acresAnnual stockpile days 365 days/yearIron oxide lumps silt content 1.7 wt. % AP-42; Table 13.2.4-1, Taconite Mining and Processing (Pellets); 11/06 (Used 1/2 value)Threshold wind speed 23 % of time % of time that wind speed exceeds 12 mph at 10 m for Toledo airport dataDays with >0.01" precipitation 120 days/yr AP-42; Figure 13.2.1-2; 1/11 for Toledo, OhioCont. eff. using water or chemical stabilization 99% Ohio EPA RACM Rule Guidance Table 2.1.2-8

Stockpile wind erosion uncontrolled emission factorsPM 3.1 lb/day/acrePM10 1.5 lb/day/acrePM2.5 0.6 lb/day/acreAir Pollution Engineering Manual; p 136; Eqn. 5; AWMA; 1992

Potential to Emit:Pollutant Controlled

Lumps Stockpile Emissions (lb/hour)*

Total Emissions (tons/year)

PM 0.0002 0.00PM10 0.0001 0.00PM2.5 0.0000 0.00*Max hourly calculated by doubling the hourly rate

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IronUnits LLC

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Table C-10: Front End Loader Reclaim Oxide Lumps Fugitive Emissions (Chemical stabilization)

Emission Unit: FEL-1, Front End Loader Fugitive Emissions from Oxide Lumps Stockpile ReclaimCH2M GAD Points 29

Parameters:Oxide Lumps Reclaim by Front End Loader 28 tons/hour Assuming 8 hour operating shift

3,595 tons/yearExpected operation 160 hours/year

Front end loader travel distance 0.02 milesEmpty front end loader weight 59 tons Lower weight FEL for lumpsLoaded front end loader weight 74 tonsAverage front end loader weight 66 tonsHourly trips 2 trips/hourAnnual trips 245 trips/yearHourly travelled distance 0.038 VMT/hourAnnual travelled distance 5 VMT/yearSilt content 3.4 wt. % AP-42; Table 13.2.4-1, Taconite Mining and Processing (Pellets); 11/06Days with >0.01" precipitation 120 days/yr AP-42; Figure 13.2.1-2; 1/11 for Toledo, OhioUnpaved road chemical stabilization control efficiency 95% Ohio EPA RACM Guidance Table 2.1.1-3

Unpaved road traffic uncontrolled emission factorsHourly (lb/VMT) Annual (lb/VMT)

PM 8.16 5.48PM10 1.94 1.30PM2.5 0.19 0.13AP-42, Page 13.2.2-4 (11/2006)

Potential to Emit:Pollutant Controlled

Oxide Lumps Reclaim FEL Fugitive Emissions (lb/hour)

Emissions (tons/year)

PM 0.02 0.00PM10 0.0037 0.00PM2.5 0.0004 0.00

Annual average distance traveled by the front end loader = 50 feet one way in the storage area (unpaved surface)

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IronUnits LLC

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Table C-11: Lump Transfer from Reclaim FEL to Truck

Emission Unit: TR-9 Oxides Lumps Drop from FEL to TruckCH2M GAD Points 30

Parameters:Lump transfer rate 28 tons/hour Assuming 8 hour shift

3,595 tons/yearExpected operation 160 hours/year Assuming 80% hourly operating rateNumber of drop points 1U = mean windspeed for Toledo 9.40 mph AP-42, Table 7.1-9, 11/2006M = moisture content 2.5 % Assumed same as the oxide pellets

Oxide fines drop point uncontrolled emission factorsPM 0.00394 lb/tonPM10 0.00186 lb/tonPM2.5 0.00028 lb/tonAP-42, Page 13.2.4-3 (11/2006)

Potential to Emit:Pollutant Oxide Lumps

Drop (lb/hour)Total Emissions (tons/year)

PM 0.11 0.01PM10 0.05 0.00PM2.5 0.008 0.00

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IronUnits LLC

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Table C-12: Oxide Lumps Truck Transport Fugitive Emissions (Watering & sweeping)

Emission Unit: HR-1, Truck Transport Fugitive Emissions from Oxide Lumps TransportCH2M GAD Points 31

Parameters:Oxide lumps transport by truck 28 tons/hour Assuming max of 8 hour shift or at least 1 trip per hour

3,595 tons/year

Truck travel distance 0.08 milesEmpty truck weight 15 tons Assumed 30,000 lbLoaded truck weight 43 tons Assumed 86,000 lbAverage truck weight 29 tonsOxide Fines weight per load 28 tonsHourly trips 1 trips/hourAnnual trips 128 trips/yearHourly travelled distance 0.1 VMT/hourAnnual travelled distance 10 VMT/yearPaved road silt loading 9.7 g/m2 AP-42; Table 13.2.1-3; 1/11 for Iron and Steel ProductionDays with >0.01" precipitation 120 days/yr AP-42; Figure 13.2.1-2; 1/11 for Toledo, OhioTime between watering application for paved roads 4 hours - apply water flushing followed by sweeping (weather permitting) at 2.2 l/m2

Control efficiency for measures 95%

Paved road traffic uncontrolled emission factorsHourly (lb/VMT) Annual (lb/VMT)

PM 2.70 2.48PM10 0.54 0.50PM2.5 0.13 0.12AP-42, Page 13.2.4-3 (11/2006)

Potential to Emit:Pollutant Controlled

Oxide Lumps Truck Fugitive (lb/hour)

Emissions (tons/year)

PM 0.01 0.00PM10 0.002 0.00PM2.5 0.001 0.00

Annual average distance traveled by the truck for each trip = 0.04 miles one way on paved surface

Control of Open Fugitive Dust Sources EPA-450/3-88-008, Table 2-4 (96-0.263V)%, V = No. of Vehicles since application

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Table C-13: Transfer from Oxide Day Bins to Conveyors (Controlled)

Emission Unit: TR-10, Oxide Day Bins to Conveyors with two baghouse routed to one stackCH2M GAD Points 33

Parameters:Oxide rate to Day Bins 560 tons/hourExpected operation 7,061 hours/year 1.1 times the annual througput rate divided by hourly rateDesign exhaust volume 20,764 dscfmMaximum exhaust rate scaleup 110%Design PM grain loading 0.0025 gr/dscf BACT limit from Essar MN Permit

Potential to Emit:Pollutant Day Bins to

Conveyors with Baghouse (lb/hour)

Emissions (tons/year)

PM 0.44 1.57PM10 0.44 1.57PM2.5 0.44 1.57Assuming PM10 and PM2.5 equals PMScaled up design flow was used here

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Table C-14: Oxide Fines Conveyor Drop (Water or chemical sprays)

Emission Unit: TR-11 Oxide Fines from Conveyor to StockpileCH2M GAD Points 34

Parameters:Oxide fines transfer rate 46 tons/hour

215,680 tons/yearExpected operation 5,823 hours/year Assuming 80% hourly operating rateNumber of drop points 1U = mean windspeed for Toledo 9.40 mph AP-42, Table 7.1-9, 11/2006M = moisture content 1.5 % Assumed reasonable worst caseWater or chemical sprays control eff. 95% Ohio EPA RACM Guidance Table 2.1.3-3

Oxide fines drop point uncontrolled emission factorsPM 0.008 lb/tonPM10 0.004 lb/tonPM2.5 0.001 lb/tonAP-42, Page 13.2.4-3 (11/2006)

Potential to Emit:Pollutant Controlled Oxide

Fines Drop (lb/hour)

Total Emissions (tons/year)

PM 0.019 0.04PM10 0.009 0.02PM2.5 0.001 0.00

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Table C-15: Oxide Fines Stockpile Wind Erosion (Water or Chemical stabilization)

Emission Unit: WE-3, Wind Erosion from Oxide Fines StockpilesCH2M GAD Points 35

Parameters:Oxide Fines stockpile 5,600 tonsVoid ratio 0.1 assumed 10% voidDensity 143 lb/cf 10% higher than the iron oxidesVolume of pile Vp 87,024 cfAngle of repose 20 degrees http://www.ckit.co.za/secure/misc/trajectories_material.htmlNumber of stockpiles 1Diameter of stockpile 122 feetHeight of stockpile 23 feet Using angle of repose and pile widthVolume of conical part of stockpile 89,975 cf =pi*(d/2)^2*h/3Stockpile Area 0.27 acresAnnual stockpile days 365 days/yearIron oxide fines silt content 3.4 wt. % AP-42; Table 13.2.4-1, Taconite Mining and Processing (Pellets); 11/06Threshold wind speed 23 % of time % of time that wind speed exceeds 12 mph at 10 m for Toledo airport dataDays with >0.01" precipitation 120 days/yr AP-42; Figure 13.2.1-2; 1/11 for Toledo, OhioCont. eff. using water or chemical stabilization 99% Ohio EPA RACM Guidance Table 2.1.2-8

Stockpile wind erosion uncontrolled emission factorsPM 6.2 lb/day/acrePM10 3.1 lb/day/acrePM2.5 1.2 lb/day/acreAir Pollution Engineering Manual; p 136; Eqn. 5; AWMA; 1992

Potential to Emit:Pollutant Controlled

Oxide Fines Stockpile Emissions (lb/hour)*

Total Emissions (tons/year)

PM 0.001 0.00PM10 0.0007 0.00PM2.5 0.0003 0.00*Max hourly calculated by doubling the hourly rate

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Table C-16: Front End Loader Reclaim Oxide Fines Fugitive Emissions (Chemical stabilization)

Emission Unit: FEL-2, Front End Loader Fugitive Emissions from Oxide Fines Stockpile ReclaimCH2M GAD Points 36

Parameters:Oxide Fines Reclaim by Front End Loader 28 tons/hour Same as truck transport frequency

215,680 tons/yearExpected operation 8,559 hours/year Assuming 90% hourly operating rate

Front end loader travel distance 0.02 milesEmpty front end loader weight 59 tons Lower weight FEL for finesLoaded front end loader weight 74 tonsAverage front end loader weight 66 tonsHourly trips 2 trips/hourAnnual trips 14,672 trips/yearHourly travelled distance 0.038 VMT/hourAnnual travelled distance 278 VMT/yearSilt content 3.4 wt. % AP-42; Table 13.2.4-1, Taconite Mining and Processing (Pellets); 11/06Days with >0.01" precipitation 120 days/yr AP-42; Figure 13.2.1-2; 1/11 for Toledo, OhioUnpaved road chemical stabilization control efficiency 95% Ohio EPA RACM Guidance Table 2.1.1-3

Unpaved road traffic uncontrolled emission factorsHourly (lb/VMT) Annual (lb/VMT)

PM 8.16 5.48PM10 1.94 1.30PM2.5 0.19 0.13AP-42, Page 13.2.2-4 (11/2006)

Potential to Emit:Pollutant Controlled Oxide

Fines FEL Fugitive (lb/hour)

Emissions (tons/year)

PM 0.02 0.04PM10 0.004 0.01PM2.5 0.0004 0.00

Annual average distance traveled by the front end loader = 50 feet one way in the storage area (unpaved surface)

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Table C-17: Fines Transfer from reclaim FEL to truck

Emission Unit: TR-12 Oxide Fines Drop from FEL to TruckCH2M GAD Points 37

Parameters:Oxide Fines transfer rate 28 tons/hour Same as truck transport frequency

215,680 tons/yearExpected operation 8,559 hours/year Assuming 90% hourly operating rateNumber of drop points 1U = mean windspeed for Toledo 9.40 mph AP-42, Table 7.1-9, 11/2006M = moisture content 1.5 % Assumed worst case moisture content

Fines drop point uncontrolled emission factorsPM 0.00805 lb/tonPM10 0.00381 lb/tonPM2.5 0.00058 lb/tonAP-42, Page 13.2.4-3 (11/2006)

Potential to Emit:Pollutant Oxide Fines Drop

(lb/hour)Total Emissions (tons/year)

PM 0.23 0.87PM10 0.11 0.41PM2.5 0.02 0.06

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Table C-18: Oxide Fines Truck Transport Fugitive Emissions (Watering & sweeping)

Emission Unit: HR-2, Truck Transport Fugitive Emissions from Oxide FinesCH2M GAD Points 38

Parameters:Oxide Fines transfer by truck 28 tons/hour Assuming max of 24 hour shift or at least 1 trip per hour

215,680 tons/year

Truck travel distance 1.14 milesEmpty truck weight 15 tons Assumed 30,000 lbLoaded truck weight 43 tons Assumed 86,000 lbAverage truck weight 29 tonsOxide Fines weight per load 28 tonsHourly trips 1 trips/hourAnnual trips 7,703 trips/yearHourly travelled distance 1.1 VMT/hourAnnual travelled distance 8,754 VMT/yearPaved road silt loading 9.7 g/m2 AP-42; Table 13.2.1-3; 1/11 for Iron and Steel ProductionDays with >0.01" precipitation 120 days/yr AP-42; Figure 13.2.1-2; 1/11 for Toledo, OhioTime between watering application for paved roads 2 hours - apply water flushing followed by sweeping (weather permitting) at 2.2 l/m2

Control efficiency for measures 95%

Paved road traffic uncontrolled emission factorsHourly (lb/VMT) Annual (lb/VMT)

PM 2.70 2.48PM10 0.54 0.50PM2.5 0.13 0.12AP-42, Page 13.2.1-4 (1/2011)

Potential to Emit:Pollutant Controlled

Oxide Fines Truck Fugitive (lb/hour)

Emissions (tons/year)

PM 0.14 0.49PM10 0.03 0.10PM2.5 0.007 0.02

Annual average distance traveled by the truck for each trip = 0.57 miles one way on paved surface

Control of Open Fugitive Dust Sources EPA-450/3-88-008, Table 2-4 (96-0.263V)%, V = No. of Vehicles since application

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Table C-19: Oxide Screen Building Operation (Controlled)

Emission Unit: SR-1, Oxide Screen with BaghouseCH2M GAD Points 39

Parameters:Oxide rate to Screen 560 tons/hourExpected operation 7,703 hours/year 1.2 times the annual througput rate divided by hourly rateDesign exhaust volume 13,278 dscfmMaximum exhaust rate scaleup 110%Design PM grain loading 0.0025 gr/dscf BACT limit from Essar MN Permit

Potential to Emit:Pollutant Controlled

Screen Baghouse (lb/hour)

Emissions (tons/year)

PM 0.28 1.10PM10 0.28 1.10PM2.5 0.28 1.10Assuming PM10 and PM2.5 equals PMScaled up design flow was used here

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Table C-20a: Iron Oxide Transfer from Conveyor to Bucket Elevator (Controlled)

Emission Unit: TR-13a, Iron Oxide Transfer to Bucket Elevator with BaghouseCH2M GAD Points 40

Parameters:Oxide rate to Core Plant 560 tons/hourExpected operation 7,703 hours/year Same as screen operationDesign exhaust volume 3,541 dscfmMaximum exhaust rate scaleup 110%Design PM grain loading 0.0025 gr/dscf BACT limit from Essar MN Permit

Potential to Emit:Pollutant Controlled

Bucket Elevator Baghouse Emissions (lb/hour)

Emissions (tons/year)

PM 0.08 0.29PM10 0.08 0.29PM2.5 0.08 0.29Assuming PM10 and PM2.5 equals PMScaled up design flow was used here

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Table C-20b: Conveyors with Fines Transfer Tower (Controlled)

Emission Unit: TR-13b, Conveyors Transfer Tower for Oxide Fines BaghouseCH2M GAD Points 81

Parameters:

Fines rate to Pile 46.30 tons/hourExpected operation 9,317 hours/year Twice the annual rate divided by hourly rateDesign exhaust volume 3,541 dscfmMaximum exhaust rate scaleup 110%Design PM grain loading 0.003 gr/dscf

Potential to Emit:Pollutant Controlled Silo

Vent and Fines Transfer Emissions (lb/hour)

Emissions (tons/year)

PM 0.08 0.35PM10 0.08 0.35PM2.5 0.08 0.35Assuming PM10 and PM2.5 equals PMScaled up design flow was used here

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Table C-21: Oxide Coating Storage and Mixing and Fines Transfer Tower (Controlled)

Emission Unit: TR-14, Oxide Coating Storage and Mixing and Fines Transfer with Common BaghouseCH2M GAD Points 4

Parameters:

Expected operation 8,760 hours/yearDesign exhaust volume 903 dscfmMaximum exhaust rate scaleup 110%Design PM grain loading 0.003 gr/dscf

Potential to Emit:Pollutant Controlled Silo

Vent and Fines Transfer Emissions (lb/hour)

Emissions (tons/year)

PM 0.02 0.08PM10 0.02 0.08PM2.5 0.02 0.08Assuming PM10 and PM2.5 equals PMScaled up design flow was used here

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Table C-22: Coating Truck Transport Fugitive Emissions (Watering & sweeping)

Emission Unit: HR-3, Truck Transport Fugitive Emissions from Oxide CoatingCH2M GAD Point 70

Parameters:Coating transfer by truck 28 tons/hour Assuming max of one truck load per hour or 8 hour truck shifts

8,987 tons/year

Truck travel distance 1.17 milesEmpty truck weight 15 tons Assumed 30,000 lbLoaded truck weight 43 tons Assumed 86,000 lbAverage truck weight 29 tonsCoating weight per load 28 tonsHourly trips 1 trips/hourAnnual trips 321 trips/yearHourly travelled distance 1.2 VMT/hourAnnual travelled distance 377 VMT/yearPaved road silt loading 9.7 g/m2 AP-42; Table 13.2.1-3; 1/11 for Iron and Steel ProductionDays with >0.01" precipitation 120 days/yr AP-42; Figure 13.2.1-2; 1/11 for Toledo, OhioTime between watering application for paved roads 4 hours - apply water flushing followed by sweeping (weather permitting) at 2.2 l/m2

Control efficiency for measures 95%

Paved road traffic uncontrolled emission factorsHourly (lb/VMT) Annual (lb/VMT)

PM 2.70 2.48PM10 0.54 0.50PM2.5 0.13 0.12AP-42, Page 13.2.1-4 (1/2011)

Potential to Emit:Pollutant Controlled

Cement Truck Fugitive (lb/hour)

Emissions (tons/year)

PM 0.16 0.02PM10 0.032 0.00PM2.5 0.008 0.00

Annual average distance traveled by the truck for each trip = 0.59 miles one way on paved surface

Control of Open Fugitive Dust Sources EPA-450/3-88-008, Table 2-4 (96-0.263V)%, V = No. of Vehicles since application

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Table C-23: REMET Conveyor Drop

Emission Unit: TR-15 REMET Conveyor to StockpileCH2M GAD Point 62

Parameters:REMET transfer rate 17 tons/hour

107,840 tons/yearExpected operation 8,024 hours/year Assuming 80% hourly operating rateNumber of drop points 1U = mean windspeed for Toledo 9.40 mph AP-42, Table 7.1-9, 11/2006M = moisture content 1.5 % Assumed worst case moisture content

REMET drop point uncontrolled emission factorsPM 0.00805 lb/tonPM10 0.00381 lb/tonPM2.5 0.00058 lb/tonAP-42, Page 13.2.4-3 (11/2006)

Potential to Emit:Pollutant REMET Drop

(lb/hour)Total Emissions (tons/year)

PM 0.14 0.43PM10 0.0640 0.21PM2.5 0.0097 0.03

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Table C-24: REMET Stockpile Wind Erosion (Windshield)

Emission Unit: WE-4, Wind Erosion from REMET Stockpiles (equipped with wind break enclosure)CH2M GAD Points 63

Parameters:REMET stockpile 6,700 tonsVoid ratio 0.1 assumed 10% voidDensity 143 lb/cf 10% higher than the iron oxidesVolume of pile Vp 104,118 cfAngle of repose 33 degreesNumber of stockpiles 1Diameter of stockpile 107 feetHeight of stockpile 35 feet Using angle of repose and pile widthVolume of conical part of stockpile 104,894 cf =pi*(d/2)^2*h/3Stockpile Area 0.21 acresAnnual stockpile days 365 days/yearREMET silt content 3.4 wt. % AP-42; Table 13.2.4-1, Taconite Mining and Processing (Pellets); 11/06Threshold wind speed 23 % of time % of time that wind speed exceeds 12 mph at 10 m for Toledo airport dataDays with >0.01" precipitation 120 days/yr AP-42; Figure 13.2.1-2; 1/11 for Toledo, OhioControl efficiency for three sided windshield 30% Ohio EPA RACM Guidance Table 2.1.2-8 (for wind break)

Stockpile wind erosion uncontrolled emission factorsPM 6.2 lb/day/acrePM10 3.1 lb/day/acrePM2.5 1.2 lb/day/acreAir Pollution Engineering Manual; p 136; Eqn. 5; AWMA; 1992

Potential to Emit:Pollutant Controlled

REMET Stockpile Emissions (lb/hour)*

Total Emissions (tons/year)

PM 0.08 0.17PM10 0.038 0.08PM2.5 0.015 0.03*Max hourly calculated by doubling the hourly rate

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Table C-25: Front End Loader Reclaim Fugitive Emissions (Cheminal stablization)

Emission Unit: FEL-3, Front End Loader Fugitive Emissions from REMET Stockpile ReclaimCH2M GAD Points 64, 65

Parameters:REMET Reclaim by Front End Loader 29 tons/hour Maximum of generation rate or 2 trips per hour

107,840 tons/yearExpected operation 4,585 hours/year

Front end loader travel distance 0.42 milesEmpty front end loader weight 59 tons Lower weight FEL for REMET transferLoaded front end loader weight 74 tonsAverage front end loader weight 66 tonsHourly trips 2 trips/hour Assuming 2 trips per hourAnnual trips 7,336 trips/yearHourly travelled distance 0.833 VMT/hourAnnual travelled distance 3,057 VMT/yearSilt content 3.4 wt. % AP-42; Table 13.2.4-1, Taconite Mining and Processing (Pellets); 11/06Days with >0.01" precipitation 120 days/yr AP-42; Figure 13.2.1-2; 1/11 for Toledo, OhioUnpaved road chemical stablization control efficiency 95% Ohio EPA RACM Guidance Table 2.1.1-3

Unpaved road traffic uncontrolled emission factorsHourly (lb/VMT) Annual (lb/VMT)

PM 8.16 5.48PM10 1.94 1.30PM2.5 0.19 0.13AP-42, Page 13.2.2-4 (11/2006)

Potential to Emit:Pollutant Controlled

REMET FEL Fugitive (lb/hour)

Emissions (tons/year)

PM 0.34 0.42PM10 0.08 0.10PM2.5 0.008 0.01

Annual average distance traveled by the front end loader = 1100 feet one way in the storage area (mix of paved and unpaved surface)

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Table C-26: REMET Transfer from FEL to Hopper

Emission Unit: TR-16, REMET from FEL to HopperCH2M GAD Points 66

Parameters:REMET transfer rate 29 tons/hour

107,840 tons/yearExpected operation 4,585 hours/year Assuming 80% hourly operating rateNumber of drop points 1U = mean windspeed for Toledo 9.40 mph AP-42, Table 7.1-9, 11/2006M = moisture content 1.5 % Assumed worst case moisture content

REMET drop point uncontrolled emission factorsPM 0.008 lb/tonPM10 0.0038 lb/tonPM2.5 0.00058 lb/tonAP-42, Page 13.2.4-3 (11/2006)

Potential to Emit:Pollutant REMET Drop

(lb/hour)Total Emissions (tons/year)

PM 0.24 0.43PM10 0.11 0.21PM2.5 0.017 0.03

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Table C-27: Three Conveyor Transfer Towers for HBI (Controlled)

Emission Unit: TR-17, TR-18 Three HBI Conveyors Transfer Towers with One Scrubber and One BaghouseCH2M GAD Points 42, 43

Parameters:HBI Throughput 510 tons/hour From design sheetExpected operation 5,833 hours/year 1.2 times the annual rate divided by hourlyDesign exhaust volume 5,331 dscfm For scrubber and baghouseMaximum exhaust rate scaleup 110%Design PM grain loading 0.0025 gr/dscf BACT limit from Essar MN Permit

Potential to Emit:Pollutant Scrubber for

HBI Transfer Tower I (lb/hour)

Baghouse for HBI Transfer Tower II & III (lb/hour)

Total Emissions (tons/year)

PM 0.11 0.11 0.67PM10 0.11 0.11 0.67PM2.5 0.11 0.11 0.67Assuming PM10 and PM2.5 equals PMScaled up design flow was used here

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Table C-28: HBI Conveyor to Stacker (Windshield)

Emission Unit: TR-19, Drop from Conveyor to Stacker ConveyorCH2M GAD Point 45

Parameters:HBI transfer rate 510 tons/hour From design sheet

2,479,080 tons/yearExpected operation 6,076 hours/year Assuming 80% hourly operating rateNumber of drop points 1U = mean windspeed 1 mph Windshield around the transfer to reduce wind effectM = moisture content 1.5 % Assumed worst case moisture content

Particle Size fraction HBI drop point emission factorsPM 0.000 lb/ton*PM10 16% 0.00007 lb/ton**PM2.5 7% 0.00003 lb/ton***PM emission factor as AP-42, Page 13.2.4-3 (11/2006)**HBI Tumble Tests from 4/2017

Potential to Emit:Pollutant HBI Conveyor to

Stacker (lb/hour)Total Emissions (tons/year)

PM 0.22 0.54PM10 0.04 0.09PM2.5 0.02 0.04

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Table C-29: HBI Stacker Conveyor to Stockpile (Water or chemical sprays)

Emission Unit: TR-20, Drop from Stacker Conveyor to StockpileCH2M GAD Point 46

Parameters:HBI transfer rate 510 tons/hour

2,479,080 tons/yearExpected operation 6,076 hours/year Same as conveyor to stackerNumber of drop points 1U = mean windspeed for Toledo 9.40 mph AP-42, Table 7.1-9, 11/2006M = moisture content 1 % AssumedWater or chemical sprays control eff. 95% Ohio EPA RACM Guidance Table 2.1.3-3

Particle Size fraction HBI drop point emission factorsPM 0.014 lb/tonPM10 16% 0.0023 lb/tonPM2.5 7% 0.0010 lb/ton*PM emission factor as AP-42, Page 13.2.4-3 (11/2006)**HBI Tumble Tests from 4/2017

Potential to Emit:Pollutant Controlled HBI

Stacking (lb/hour)

Total Emissions (tons/year)

PM 0.36 0.88PM10 0.06 0.14PM2.5 0.03 0.06

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Table C-30: HBI Stockpile Wind Erosion (Water or Chemical stabilization)

Emission Unit: WE-5, Wind Erosion from HBI StockpilesCH2M GAD Point 47

Parameters:HBI stockpile 111,000 tonsVoid ratio 0.15 assumed 15% voidHBI density 169 lb/cfVolume of pile Vp 1,549,597 cfAngle of repose 20 degrees http://www.ckit.co.za/secure/misc/trajectories_material.htmlNumber of stockpiles 1Width of stockpile 100 feetHeight of stockpile 18 feet Using angle of repose and pile widthVolume of conical part of stockpile 47,124 cf =pi*(d/2)^2*h/3Remaining volume in triangle section 1,502,473 cf Calculated for one pileLength of triangle section of stockpile 1670 feet Volume of prism = 1/2*a*c*hStockpile Area 4.02 acres Area for 1 pileAnnual stockpile days 365 days/yearHBI silt content 1.5 wt. % Engineering estimate for the manufactured briquettesThreshold wind speed 23 % of time % of time that wind speed exceeds 12 mph at 10 m for Toledo airport dataDays with >0.01" precipitation 120 days/yr AP-42; Figure 13.2.1-2; 1/11 for Toledo, OhioCont. eff. using water or chemical stabilization 99% Ohio EPA RACM Guidance Table 2.1.2-8

Stockpile wind erosion uncontrolled emission factorsPM 2.7 lb/day/acrePM10 1.4 lb/day/acrePM2.5 0.5 lb/day/acreAir Pollution Engineering Manual; p 136; Eqn. 5; AWMA; 1992

Potential to Emit:Pollutant Controlled

HBI Stockpile Emissions (lb/hour)*

Emissions (tons/year)

PM 0.01 0.02PM10 0.005 0.01PM2.5 0.002 0.00*Max hourly calculated by doubling the hourly rate

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Table C-31: Front End Loader HBI Reclaim Fugitive Emissions (Chemical stabilization)

Emission Unit: FEL-4, Front End Loader Fugitive Emissions from HBI Stockpile ReclaimGAD Point 93

Parameters:HBI Reclaim by Front End Loader 510 tons/hour From design sheet

500,000 tons/year Assuming maximum 20% reclaim by FELExpected operation 1,634 hours/year Assuming 60% operating rate

Front end loader travel distance 0.04 milesEmpty front end loader weight 118 tonsLoaded front end loader weight 154 tonsAverage front end loader weight 136 tonsHourly trips 14 trips/hourAnnual trips 14,006 trips/yearHourly travelled distance 0.541 VMT/hourAnnual travelled distance 531 VMT/yearSilt content 3.4 wt. % AP-42; Table 13.2.4-1, Taconite Mining and Processing (Pellets); 11/06Days with >0.01" precipitation 120 days/yr AP-42; Figure 13.2.1-2; 1/11 for Toledo, OhioUnpaved road chemical stabilization control efficiency 95% Ohio EPA RACM Guidance Table 2.1.1-3

Unpaved road traffic uncontrolled emission factorsHourly (lb/VMT) Annual (lb/VMT)

PM 11.27 7.57PM10 2.68 1.80PM2.5 0.27 0.18AP-42, Page 13.2.2-4 (11/2006)

Potential to Emit:Pollutant Controlled HBI

FEL Fugitive (lb/hour)

Emissions (tons/year)

PM 0.30 0.10PM10 0.07 0.02PM2.5 0.007 0.00

Annual average distance traveled by the front end loader = 100 feet one way in the storage area (unpaved surface)

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Table C-32a: HBI Bucket Wheel Reclaim to Conveyor (Water or chemical sprays)

Emission Unit: TR-21a, Reclaim HBI using Bucket Wheel to Conveyor using Sprays with ChemicalsCH2M GAD Point 48

Parameters:HBI transfer rate from reclaim 800 tons/hour 24-hour average rate for this operation

19,200 tons/day2,479,080 tons/year

Expected operation 5,165 hours/year Assuming 60% operating rateNumber of controlled drop points 1U = mean windspeed for Toledo 9.40 mph AP-42, Table 7.1-9, 11/2006M = moisture content 1.5 % Assumed worst case moisture contentWater or chemical sprays control eff. 95% Ohio EPA RACM Guidance Table 2.1.3-3

Oxide drop point (open) emission factorsPM 0.008 lb/tonPM10 16% 0.0013 lb/tonPM2.5 7% 0.0006 lb/ton*PM emission factor as AP-42, Page 13.2.4-3 (11/2006)**HBI Tumble Tests from 4/2017

Potential to Emit:Pollutant Controlled

Transfer from Reclaim Bucket to Conveyor (lb/hour)

Total Emissions (tons/year)

PM 0.32 0.50PM10 0.05 0.08PM2.5 0.02 0.03

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Table C-32b: Conveyor from Reclaim Machine to Main Conveyor (Windshield)

Emission Unit: TR-21b, HBI Conveyor from Reclaim Machine to Conveyor with WindshieldCH2M GAD Points 49

Parameters:HBI transfer rate from reclaim 800 tons/hour

2,479,080 tons/yearExpected operation 5,165 hours/year Assuming 60% operating rateNumber of controlled drop points 1U = mean windspeed 1 mph Windshield around the transfer to reduce wind effectM = moisture content 1.5 % Assumed worst case moisture content

Oxide drop point (open) emission factorsPM 0.0004 lb/tonPM10 16% 0.0001 lb/tonPM2.5 7% 0.0000 lb/ton*PM emission factor as AP-42, Page 13.2.4-3 (11/2006)**HBI Tumble Tests from 4/2017

Potential to Emit:Pollutant Transfer from

Reclaim to Conveyor (lb/hour)

Total Emissions (tons/year)

PM 0.35 0.54PM10 0.06 0.09PM2.5 0.02 0.04No control efficiency is applied

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Table C-32c: HBI FEL Two Reclaim FEL Drop to Hoppers (controlled)

Emission Unit: TR-21c FEL Reclaim Drop to Hoppers with water or chemical spraysCH2M GAD Point 50/51 (note 52 and 53 are on rails and will have no emissions)

Parameters:HBI transfer rate 510 tons/hour

500,000 tons/yearExpected operation 1,634 hours/year Assuming 60% hourly operating rateNumber of drop points 1 HBI drop to one of two (2) hoppersU = mean windspeed for Toledo 9.40 mph AP-42, Table 7.1-9, 11/2006M = moisture content 1.5 % Assumed worst case moisture contentWater or chemical sprays control eff. 95% Ohio EPA RACM Guidance Table 2.1.3-3

Particle Size fraction HBI drop point emission factorsPM 0.0080 lb/ton*PM10 16% 0.00129 lb/ton**PM2.5 7% 0.00056 lb/ton***PM emission factor as AP-42, Page 13.2.4-3 (11/2006)**HBI Tumble Tests from 4/2017

Potential to Emit:Pollutant Controlled HBI

Drop (lb/hour)Total Emissions (tons/year)

PM 0.21 0.10PM10 0.03 0.02PM2.5 0.01 0.01

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Table C-33: HBI Two Reclaim Hoppers to Conveyors (Windshield)

Emission Unit: TR-22 Two Reclaim Hopper Drop to Conveyor inside EnclosureCH2M GAD Point 54/55

Parameters:HBI transfer rate 510 tons/hour

500,000 tons/yearExpected operation 1,634 hours/year Same as hoppersNumber of drop points 1 HBI drop to one of two (2) hoppersU = mean windspeed 1 mph Hopper to conveyor will occur inside an enclosureM = moisture content 1.5 % Assumed worst case moisture content

Particle Size fraction HBI drop point emission factorsPM 0.00044 lb/ton*PM10 16% 0.00007 lb/ton**PM2.5 7% 0.00003 lb/ton***PM emission factor as AP-42, Page 13.2.4-3 (11/2006)**HBI Tumble Tests from 4/2017

Potential to Emit:Pollutant HBI Drop

Conveyor (lb/hour)

Total Emissions (tons/year)

PM 0.22 0.11PM10 0.04 0.02PM2.5 0.02 0.01

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Table C-34: HBI Conveyor to Transfer Tower (Controlled)

Emission Unit: TR-23 HBI Conveyor from Transfer Tower to HBI Loadout Building with BaghouseCH2M GAD Point 56

Parameters:HBI Throughput 800 tons/hourExpected operation 5,165 hours/year Same as TR-21bDesign exhaust volume 3,281 dscfmMaximum exhaust rate scaleup 110%Design PM grain loading 0.0025 gr/dscf BACT limit from Essar MN Permit

Potential to Emit:Pollutant Controlled for

HBI Transfer Tower (lb/hour)

Total Emissions (tons/year)

PM 0.07 0.18PM10 0.07 0.18PM2.5 0.07 0.18Assuming PM10 and PM2.5 equals PMScaled up design flow was used here

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Table C-35: HBI Conveyor to Loading (Controlled)

Emission Unit: TR-24 HBI Conveyor Transfer from Conveyor to Loading Bin with BaghouseCH2M GAD Point 57

Parameters:HBI Throughput 800 tons/hourExpected operation 4,380 hours/year 50% annual operating timeDesign exhaust volume 3,281 dscfmMaximum exhaust rate scaleup 110%Design PM grain loading 0.0025 gr/dscf BACT limit from Essar MN Permit

Potential to Emit:Pollutant Baghouse for

Conveyors to Loadout (lb/hour)

Total Emissions (tons/year)

PM 0.07 0.15PM10 0.07 0.15PM2.5 0.07 0.15Assuming PM10 and PM2.5 equals PMScaled up design flow was used here

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Table C-36: HBI Conveyor to Loading (Controlled)

Emission Unit: TR-25 HBI Loadout for Truck and Building Evacuation with BaghouseCH2M GAD Point 59

Parameters:HBI Throughput 500 tons/hour From the trucks sheetExpected operation 8,760 hours/year 2 times the annual rateDesign exhaust volume 4,920 dscfmMaximum exhaust rate scaleup 110%Design PM grain loading 0.0025 gr/dscf BACT limit from Essar MN Permit

Potential to Emit:Pollutant Baghouse for

Truck Loadout (lb/hour)

Total Emissions (tons/year)

PM 0.11 0.46PM10 0.11 0.46PM2.5 0.11 0.46Assuming PM10 and PM2.5 equals PMScaled up design flow was used here

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Table C-37a: HBI Drop to Rail Fugitive Portion Escaping the Capture System

Emission Unit: TR-26 HBI Drop to RailCH2M GAD Point 58 Rail

Parameters:HBI transfer rate 12,000 tons/day (Assume two trains per day operation for seven days per week)HBI transfer rate daily average 500 tons/hour 24-hour rate

2,479,080 tons/yearExpected operation 2,556 hours/year Assuming 80% hourly operating rateNumber of drop points 1 Assuming all HBI being transferred through trainU = mean windspeed 1 mph Drop to train will occur inside a loadout buidling covered with curtains with loadout chuteM = moisture content 1.5 % Assumed worst case moisture contentControl efficiency for water sprays for Trains 95% Ohio EPA RACM Guidance Table 2.1.3-3

Particle Size fraction HBI drop point emission factorsPM 0.0004 lb/ton*PM10 16% 0.00007 lb/ton**PM2.5 7% 0.00003 lb/ton***PM emission factor as AP-42, Page 13.2.4-3 (11/2006)**HBI Tumble Tests from 4/2017

Potential to Emit:Pollutant Fugitive HBI

Drop Train (lb/hour)

Total Emissions (tons/year)

PM 0.01 0.03PM10 0.002 0.00PM2.5 0.001 0.00

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Table C-37b: HBI Drop to Truck Fugitive Portion Escaping the Capture System

Emission Unit: TR-27, HBI Drop to TruckCH2M GAD Point Truck Building 83

Parameters:HBI transfer rate 500 tons/hour Assuming 12-hour shiftHBI transfer rate daily average 250 tons/hour 24-hour rate based on 12-hour shift

6,000 tons/day2,190,000 tons/year

Expected operation 5,475 hours/year Assuming 80% hourly operating rateNumber of drop points 1 Assuming all HBI being transferred through only one transfer to truckU = mean windspeed 1 mph Drop to truck will occur inside a loadout buidling with loadout chuteM = moisture content 1.5 % Assumed worst case moisture contentHBI Transfer to Truck 55%Capture efficiency of building for Trucks 95% Assumed since building equipped with garage doors on both sides

Particle Size fraction HBI drop point emission factorsPM 0.0004 lb/ton*PM10 16% 0.00007 lb/ton**PM2.5 7% 0.00003 lb/ton***PM emission factor as AP-42, Page 13.2.4-3 (11/2006)**HBI Tumble Tests from 4/2017

Potential to Emit:Pollutant Fugitive HBI

Drop Truck (lb/hour)

Total Emissions (tons/year)

PM 0.005 0.02PM10 0.0009 0.00PM2.5 0.0004 0.00

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Table C-38: HBI Truck Transport Fugitive Emissions (Watering & sweeping)

Emission Unit: HR-4, Truck Transport Fugitive Emissions from HBICH2M GAD Point 60

Parameters:HBI transfer by truck maximum hourly 500 tons/hour Max traffic at 10 trucks per hourHBI transfer by truck daily average 250 tons/hour 24-hour rate based on 12-hour shift

2,190,000 tons/yearAnnual truck transfer operations 4,380 hours/year

Truck travel distance 0.79 milesEmpty truck weight 25 tons Assumed use of 50,000 lb Michigan double trucksLoaded truck weight 75 tonsAverage truck weight 50 tons Assumed conservatively that truck loading will occur at halfway pointHBI weight per load 50 tons For Michigan double trucksHourly trips for control purposes 10 trips/hour Using maximum hourlyHourly trips for daily emissions 5 trips/hour Using daily rateAnnual trips 43,800 trips/yearHourly travelled distance 3.9 VMT/hour Using daily rateAnnual travelled distance 34,427 VMT/yearPaved road silt loading 9.7 g/m2 AP-42; Table 13.2.1-3; 1/11 for Iron and Steel ProductionDays with >0.01" precipitation 120 days/yr AP-42; Figure 13.2.1-2; 1/11 for Toledo, OhioTime between watering application for paved roads 0.25 hours - apply water flushing followed by sweeping (weather permitting) at 2.2 l/m2

Control efficiency for measures 95%

Paved road traffic uncontrolled emission factorsHourly (lb/VMT) Annual (lb/VMT)

PM 4.70 4.32PM10 0.94 0.86PM2.5 0.23 0.21AP-42, Page 13.2.1-4 (1/2011)

Potential to Emit:Pollutant Controlled HBI

Truck Fugitive (lb/hour)

Emissions (tons/year)

PM 0.86 3.46PM10 0.17 0.69PM2.5 0.04 0.17

Annual average distance traveled by the truck for each trip = 0.39 miles one way on paved surface

Control of Open Fugitive Dust Sources EPA-450/3-88-008, Table 2-4 (96-0.263V)%, V = Vehicles since application

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Table C-39a: Furnace Feed Conveyor (Controlled)

Emission Unit: TR-28a Transfer from Oxide Conveyor to Furnace Feed Conveyor with BaghouseGAD Point 91

Parameters:Oxide rate to Core Plant 560 tons/hourExpected operation 7,703 hours/year Same as screen operationDesign exhaust volume 2,918 dscfmMaximum exhaust rate scaleupDesign PM grain loading 0.0025 gr/dscf BACT limit from Essar MN Permit

Potential to Emit:Pollutant Baghouse for

Conveyors to Loadout (lb/hour)

Total Emissions (tons/year)

PM 0.06 0.24PM10 0.06 0.24PM2.5 0.06 0.24Assuming PM10 and PM2.5 equals PM

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Table C-39b: Furnace Charge Hopper (Controlled)

Emission Unit: TR-28b, Furnace Charge Hopper ScrubberCH2M GAD Point 3

Parameters:Oxide Throughput 560 tons/hourExpected operation 8,760 hours/yearDesign exhaust volume 1,579 scfmMaximum exhaust rate scaleup 100%Design PM grain loading 0.007 gr/dscfNOx 178.3 ppmSO2 15.3 ppmCO 410 ppmCO2 124,320 ppm

Potential to Emit:Pollutant Scrubber for

Charge Hopper (lb/hour)

Emissions (tons/year)

PM 0.10 0.44PM10 0.10 0.44PM2.5 0.10 0.44NOx 2.02 8.85SO2 0.24 1.05CO 2.82 12.36CO2 1,345 5,891CO2e 1,345 5,891Assuming PM10 and PM2.5 equals PM

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Table C-40: Bottom Seal Gas Scrubber Exhaust (Controlled)

Emission Unit: P-1, Bottom Seal Gas Scrubber ExhaustCH2M GAD Point 2

Parameters:Oxide Throughput 320 tons/hourExpected operation 8,760 hours/yearDesign exhaust volume 40,349 scfmMaximum exhaust rate scaleup 100%Design PM (filt.) grain loading 0.007 gr/dscfPM (condensable) 0.00015 gr/dscfNOx 1.5 ppmSO2 0.6 ppmCO 5606 ppmCO2 3,028 ppm

Potential to Emit:Pollutant Bottom Seal

Gas Scrubber (lb/hour)

Emissions (tons/year)

PM 2.56 11.21PM10 2.61 11.44PM2.5 2.61 11.44NOx 0.43 1.88SO2 0.24 1.05CO 986.03 4318.80CO2 837 3,666CO2e 837 3,666Assuming PM10 and PM2.5 equals PMRevised rates

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Table C-41: Reformer Flue Gas Exhaust

Emission Unit: P-2, Reformer Flue Gas ExhaustCH2M GAD Point 1

Parameters:Expected operation 8,760 hours/yearNatural gas heat input 337 MMBtu/hourHBI throughput 316 tons/hourDesign exhaust volume 305,347 scfmMaximum exhaust rate scaleup 100%Design PM (filt.) grain loading 0.0031 gr/dscfPM (condensable) 0.0041 gr/dscfDesign PM (filt.) 0.005 lb/MMBtuDesign PM (filt.+cond.) 0.012 lb/MMBtuNOx 46 ppm LNBSO2 1.7 ppmCO 39 ppmVOC 0.0054 lb/MMBtu AP-42CO2 169,573 ppm

Potential to Emit:Pollutant Reformer

Exhaust (lb/hour)

Emissions (tons/year)

PM 8.06 35.30PM10 18.71 81.96PM2.5 18.71 81.96NOx 99.75 436.89SO2 5.05 22.12CO 52.35 229.29VOC 1.82 7.97CO2 354,764 1,553,868CO2e 354,805 1,554,047Revised rates

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Table C-42: Hot Briquette Exhaust (Controlled)

Emission Unit: P-3, Hot Briquette Scrubber ExhaustCH2M GAD Point 5

Parameters:HBI Throughput 320 tons/hourExpected operation 8,760 hours/yearDesign exhaust volume 63,228 scfmMaximum exhaust rate scaleup 100%Design PM (filt.) grain loading 0.0073 gr/dscfPM (condensable) 0.00024 gr/dscfNOx 8.7 ppmSO2 0.3 ppmCO 3309 ppmCO2 28,497 ppm

Potential to Emit:Pollutant Hot Briquette

Scrubber Exhaust (lb/hour)

Emissions (tons/year)

PM 3.97 17.39PM10 4.10 17.96PM2.5 4.10 17.96NOx 3.94 17.25SO2 0.21 0.92CO 912.01 3994.62CO2 12,345 54,071CO2e 12,345 54,071Assuming PM10 and PM2.5 equals PMRevised rates

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Table C-43: Briquette Cooling System Vapor Removal Vent Pipe (Controlled)

Emission Unit: P-4, Briquette Cooling System Vapor Removal Vent Pipe ScrubberCH2M GAD Point 6

Parameters:HBI Throughput 320 tons/hourExpected operation 8,760 hours/yearDesign exhaust volume 50,532 scfmMaximum exhaust rate scaleup 100%Design PM grain loading 0.008 gr/dscfCO 2,697 ppmvd

Potential to Emit:Pollutant Briquette

Cooling System Vent (lb/hour)

Emissions (tons/year)

PM 3.30 14.47PM10 3.30 14.47PM2.5 3.30 14.47CO 594.08 2,602.05Assuming PM10 and PM2.5 equals PMRevised rates

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Table C-44: Degasser Exhaust

Emission Unit: P-5, Degasser ExhaustCH2M GAD Point 7

Parameters:Expected operation 8,760 hours/yearDesign exhaust volume 15,002 scfmMaximum exhaust rate scaleup 100%CO 1,683 ppmvCO2 40,103 ppmvNH3 100 ppmv Estimated

Potential to Emit:Pollutant Degasser

Exhaust (lb/hour)

Emissions (tons/year)

CO 110.06 482.05CO2 4,122.00 18,054NH3 3.97 17.39Revised rates

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Table C-45a: Flare During Shutdown/Startup/Upset

Emission Unit: P-6a, Flare operation during Shutdown/Startup/UpsetCH2M GAD Point 9a

Parameters:Number of events 24 #/yearShutdown/Startup flaring duration 4 hours Assumed 2 hour eachFlow of gas to flare 99,520 scfm MIDREX dataHeat release rate 1,678 MMBtu/hour Based on 1,525 MMBtu/hour (LHV) MIDREX dataGas heating value 272 Btu/scf From GoWest applicationHeat input from gas 1,624 MMBtu/hourMaximum rate scaleup 110%

PM (filterable) 0.0019 lb/MMBtu AP-42 for NG CombustionPM (condensable) 0.0056 lb/MMBtu AP-42 for NG CombustionNOx 0.068 lb/MMBtu AP-42 for FlareSO2 0.0006 lb/MMBtu AP-42 for NG CombustionCO 0.310 lb/MMBtu AP-42 for FlareVOC 0.0518 lb/MMBtu AP-42 for FlareCO2 117 lb/MMBtu 40 CFR Part 98CO2e 117 lb/MMBtu 40 CFR Part 98

Potential to Emit:Pollutant Flare

(lb/hour) (Annual avg.)

Emissions (tons/year)

PM 0.04 0.16PM10 0.15 0.64PM2.5 0.15 0.64NOx 1.33 5.83SO2 0.01 0.05CO 6.07 26.58VOC 1.01 4.44CO2 2,290 10,031CO2e 2,293 10,042For filterable fraction, assuming PM10 and PM2.5 equals PMScaled up design flow was used hereRevised rates

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Table C-45b: Flare (Pilot Only)

Emission Unit: P-6b, Flare (Pilot Only)CH2M GAD Point 9b

Parameters:Expected operation 8,760 hours/yearNatural gas heat input 0.72 MMBtu/hourDesign exhaust volume 105 scfmMaximum exhaust rate scaleup 100%PM (filterable) 0.0019 lb/MMBtu AP-42 for NG CombustionPM (condensable) 0.0056 lb/MMBtu AP-42 for NG CombustionNOx 0.068 lb/MMBtu AP-42 for FlareSO2 0.0006 lb/MMBtu AP-42 for NG CombustionCO 0.310 lb/MMBtu AP-42 for FlareVOC 0.0518 lb/MMBtu AP-42 for FlareCO2 117 lb/MMBtu 40 CFR Part 98CO2e 117 lb/MMBtu 40 CFR Part 98

Potential to Emit:Pollutant Flare Pilot

(lb/hour)Emissions (tons/year)

PM 0.001 0.01PM10 0.005 0.02PM2.5 0.005 0.02NOx 0.049 0.22SO2 0.000 0.00CO 0.224 0.98VOC 0.037 0.16CO2 85 371CO2e 85 371For filterable fraction, assuming PM10 and PM2.5 equals PM

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Table C-46: Cooling Tower (Controlled)

Emission Unit: P-7, Cooling Tower with Drift EliminatorCH2M GAD Point 8

Parameters:Circulation water flow rate 24,766 gal/minTDS circulating water 1,100 ppmwTotal drift loss 0.0005%Operating time 8,760 hour/yearParticle size multiplier*

PM 1PM10 0.3150PM2.5 0.1890

Potential to Emit:Pollutant Cooling

Tower (lb/hour)

Emissions (tons/year)

PM 0.07 0.30PM10 0.02 0.09PM2.5 0.01 0.06VOC (Chloroform)** 0.12NH3*** 2.25 9.86**From Cooling Tower HAPs calculations***NH3 emission rate is an engineering estimate

*PM10 and PM2.5 emission factors from the TDS for APS Ocotillo Permit No.V95-007, PSD16-01, March 22, 2016, Maricopa County AQD.

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Table C-47: Fire Water Booster

Emission Unit: P-8, Emergency Diesel Fire Water Booster 311 bhpCH2M GAD Point 10

Parameters:Expected operation 500 hours/yearPower Output 311 bhp Standby rating

232 kWFuel Use Rate 18 gal/hourDiesel heating value 138000 Btu/gallon 40 CFR Part 98 Table C-1Heat Input Rate 2.42 MMBtu/hourPM 0.2 g/kW-hr Filterable only from NSPS IIIIPM10 0.24 g/kW-hr Filterable from PM and Condensable from AP-42PM2.5 0.24 g/kW-hr Same as PM10NOx 4.0 g/kW-hr NSPS Subpart IIII Table 4 (assumed no HC)SO2 0.007 g/kW-hr Assuming 15 ppm sulfur fuelCO 3.5 g/kW-hr NSPS Subpart IIII Table 4VOC 0.0025 lb/hp-hr AP-42 Table 3.3-1CO2 163.05 lb/MMBtu 40 CFR Part 98 Table A-1 and C-1 and C-2CO2e 163.61 lb/MMBtu 40 CFR Part 98 Table A-1 and C-1 and C-2PM condensable 0.0077 lb/MMBtu AP-42 Table 3.4-2

Potential to Emit:Pollutant RICE Exhaust

(lb/hour)Emissions (tons/year)

PM 0.10 0.03PM10 0.12 0.03PM2.5 0.12 0.03NOx 2.05 0.51SO2 0.00 0.00CO 1.79 0.45VOC 0.78 0.20CO2 394 98CO2e 395 99Revised rates

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Table C-48: Emergency Generator Engine

Emission Unit: P-9, Emergency Generator Engine Diesel 2,682 bhpCH2M GAD Point 11

Parameters:Expected operation 500 hours/yearPower Output 2,682 bhp Standby rating

2,000 kWFuel Use Rate 121 gal/hourDiesel heating value 138000 Btu/gallon 40 CFR Part 98 Table C-1Heat Input Rate 16.70 MMBtu/hourPM 0.2 g/kW-hr Filterable only from NSPS IIII and 40 CFR 89.112(a) Tier 2PM10 0.23 g/kW-hr Filterable from PM and Condensable from AP-42PM2.5 0.23 g/kW-hr Same as PM10NOx 6.4 g/kW-hr NSPS Subpart IIII and 40 CFR 89.112(a) Tier 2 (assumed no HC)SO2 0.006 g/kW-hr Assuming 15 ppm sulfur fuelCO 3.5 g/kW-hr NSPS Subpart IIII and 40 CFR 89.112(a) Tier 2VOC 0.0006 lb/hp-hr AP-42 Table 3.4-1CO2 163.05 lb/MMBtu 40 CFR Part 98 Table A-1 and C-1 and C-2CO2e 163.61 lb/MMBtu 40 CFR Part 98 Table A-1 and C-1 and C-2PM condensable 0.0077 lb/MMBtu AP-42 Table 3.4-2

Potential to Emit:Pollutant RICE Exhaust

(lb/hour)Emissions (tons/year)

PM 0.88 0.22PM10 1.01 0.25PM2.5 1.01 0.25NOx 28.22 7.05SO2 0.03 0.01CO 15.43 3.86VOC 1.72 0.43CO2 2,723 681CO2e 2,732 683

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Table C-49: Fugitive Natural Gas Emissions From Equipment Leaks

Emission Unit: FugGHG - Emissions from Valves, Pressure Relief Valves, Connectors

CH4 EF CH4 Emissions CO2e PTE VOC PTEComponents Number* (kg/hr/#)** (tons/year) (tons/year) (tons/year)Valves - gas service 418 0.00597 23.45 0.649Pressure relief valves 54 0.104 52.77 1.462Connectors 1,982 0.00183 34.08 0.944Total 110.29 2757 3.055*Added 10% contingency to the design basis.

VOC Factor*** = 0.028 lb VOC per lb methane in transmission segment 2.70%

**Table 2-1, 1995 Protocol for Equipment Leak Emission Estimates; U.S. EPA, Emission Standards Division, Office of Air and Radiation, Office of Air Quality Planning and Standards, Research Triangle Park, North Carolina 27711; November 1995; EPA-453/R-95-017.

***Table 5-4, 2011 Oil and Natural Gas Sector: Standards of Performance for Crude Oil and Natural Gas Production, Transmission, and Distribution; U.S. EPA, Sector Policies and Programs Division, Office of Air Quality Planning and Standards, Research Triangle Park, North Carolina 27711; July 2011; EPA-453/R-11-0002.

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Table C-50: Hazardous Air Pollutants (HAPS) NG Combustion

Parameters:

Emission Unit->Reformer Exhaust

Flare (NG Pilots)

Heat Input MMBtu/hour 337 0.7Fuel Use MMscf/year 2,898 6For reformer exhaust, HAPs emissions associated with NG combustion only. Top gas is largely H2 and CO.NG HHV 1020 MMBtu/MMscf

Emission Factor Emissions (lb/hour) Emissions (tons/year)

Pollutant (lb/MMBtu) ReformerFlare (NG Pilots) Reformer

Flare (NG Pilots) Total

Arsenic compounds 1.96E-07 6.62E-05 1.42E-07 2.90E-04 6.21E-07 2.90E-04Beryllium compounds 1.18E-08 3.97E-06 8.51E-09 1.74E-05 3.73E-08 1.74E-05Cadmium compounds 1.08E-06 3.64E-04 7.80E-07 1.59E-03 3.42E-06 1.60E-03Chromium compounds 1.37E-06 4.63E-04 9.93E-07 2.03E-03 4.35E-06 2.03E-03Cobalt compounds 8.24E-08 2.78E-05 5.96E-08 1.22E-04 2.61E-07 1.22E-04Lead compounds 4.90E-07 1.65E-04 3.55E-07 7.24E-04 1.55E-06 7.26E-04Manganese compounds 3.73E-07 1.26E-04 2.69E-07 5.51E-04 1.18E-06 5.52E-04Mercury compounds 2.55E-07 8.60E-05 1.84E-07 3.77E-04 8.08E-07 3.78E-04Nickel compounds 2.06E-06 6.95E-04 1.49E-06 3.04E-03 6.52E-06 3.05E-03Selenium compounds 2.35E-08 7.94E-06 1.70E-08 3.48E-05 7.45E-08 3.48E-05Benzene 2.06E-06 6.95E-04 1.49E-06 3.04E-03 6.52E-06 3.05E-03Dichlorobenzene 1.18E-06 3.97E-04 8.51E-07 1.74E-03 3.73E-06 1.74E-03Formaldehyde 7.35E-05 2.48E-02 5.32E-05 0.11 2.33E-04 0.11Hexane 1.76E-03 5.95E-01 1.28E-03 2.61 0.01 2.61Naphthalene 6.27E-07 2.12E-04 4.54E-07 9.27E-04 1.99E-06 9.29E-04POM 6.82E-07 2.30E-04 4.94E-07 1.01E-03 2.16E-06 1.01E-03Toluene 3.33E-06 1.12E-03 2.41E-06 4.93E-03 1.06E-05 4.94E-03Single Max HAP (Hexane) 2.61 0.01 2.61Total 2.74 0.01 2.74EPA AP-42, Chapter 1.4, Tables 1.4-2, 1.4-3, 1.4-4; 7/1998.Pollutants for which AP-42 records one half the source testing detection limit have not been included.

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Table C-51: Hazardous Air Pollutants (HAPs) Emissions from Emergency Engines

Parameters: Fire Water EmergencyBooster Generator

Engine Heat Input: 2.42 16.70 MMBtu/hourMax Annual Hours: 500 500 hour/yearAnnual Heat Input: 1208 8349 MMBtu/year

Emission Factor

Firewater Booster Emissions

Generator Emissions Total

Pollutant (lb/MMBtu(tons/year) (tons/year)Benzene 7.67E-04 4.63E-04 3.20E-03PAHs (total) 2.12E-04 1.28E-04 8.85E-04Toluene 2.81E-04 1.70E-04 1.17E-03Xylene 1.93E-04 1.17E-04 8.06E-04Single Max HAP (Benzene) 4.63E-04 3.20E-03 3.66E-03Total 1.34E-03 9.27E-03 1.06E-02

EPA AP-42, Chapter 3.4, Tables 3.4-3, 3.4-4, 10/1996.

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Table C-52: Hazardous Air Pollutants (HAPs) Emissions from Cooling Tower

Parameters:

Cooling Tower2.3 kg/109 liters

Cooling tower water flow 24,766 gal/minChloroform emissions 0.03 lb/hour

0.12 tons/year

Peak Drift 0.12 gal/minBlowdown Conc.* Emissions

HAPs ppb lb/gallon tons/yearChloroform 0.12Arsenic 8.1 6.76E-08 2.2E-06Nickel 6 5.01E-08 1.63E-06Selenium 8.25 6.88E-08 2.24E-06Total 0.12*Assumed values based on other similar installations

Corrected Emission Factor for Chloroform (kg/109 liters cooling water flow) From EPA document "Locating and Estimating Air Emissions from Sources of Chloroform," page 58

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Table C-53: Feed Recovery Transfer

Emission Unit: TR-29 Feed Recovery Transfer to StockpileGAD Point 94

Parameters:Feed transfer rate 0.50 tons/hour

3,210 tons/yearExpected operation 8,024 hours/year Assuming 80% hourly operating rateNumber of drop points 1U = mean windspeed for Toledo 9.40 mph AP-42, Table 7.1-9, 11/2006M = moisture content 1.5 % Assumed worst case moisture content

Feed drop point uncontrolled emission factorsPM 0.00805 lb/tonPM10 0.00381 lb/tonPM2.5 0.00058 lb/tonAP-42, Page 13.2.4-3 (11/2006)

Potential to Emit:Pollutant Feed Drop

(lb/hour)Total Emissions (tons/year)

PM 0.004 0.01PM10 0.0019 0.01PM2.5 0.0003 0.00

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IronUnits LLC

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Table C-54: Feed Recovery Stockpile Wind Erosion (Windshield)

Emission Unit: WE-6, Wind Erosion from Feed Recovery Stockpile (equipped with wind break enclosure)GAD Points 95

Parameters:Feed Recovery stockpile 85 tonsVoid ratio 0.1 assumed 10% voidDensity 143 lb/cf 10% higher than the iron oxidesVolume of pile Vp 1,321 cfAngle of repose 33 degreesNumber of stockpiles 1Diameter of stockpile 25 feetHeight of stockpile 9 feet Using angle of repose and pile widthVolume of conical part of stockpile 1,467 cf =pi*(d/2)^2*h/3Stockpile Area 0.02 acresAnnual stockpile days 365 days/yearFeed silt content 3.4 wt. % AP-42; Table 13.2.4-1, Taconite Mining and Processing (Pellets); 11/06Threshold wind speed 23 % of time % of time that wind speed exceeds 12 mph at 10 m for Toledo airport dataDays with >0.01" precipitation 120 days/yr AP-42; Figure 13.2.1-2; 1/11 for Toledo, OhioControl efficiency for three sided windshield 30% Ohio EPA RACM Guidance Table 2.1.2-8 (for wind break)

Stockpile wind erosion uncontrolled emission factorsPM 6.2 lb/day/acrePM10 3.1 lb/day/acrePM2.5 1.2 lb/day/acreAir Pollution Engineering Manual; p 136; Eqn. 5; AWMA; 1992

Potential to Emit:Pollutant Controlled Feed

Recovery Stockpile Emissions (lb/hour)*

Total Emissions (tons/year)

PM 0.01 0.02PM10 0.004 0.01PM2.5 0.001 0.00*Max hourly calculated by doubling the hourly rate

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Table C-55: Front End Loader Reclaim Fugitive Emissions (Cheminal stablization)

Emission Unit: FEL-5, Front End Loader Fugitive Emissions from Feed Recovery Stockpile ReclaimGAD Points 96

Parameters:Feed Recovery Stockpile Reclaim by Front End Loader 15 tons/hour 1 trips per hour

3,210 tons/yearExpected operation 273 hours/year

Front end loader travel distance 0.19 milesEmpty front end loader weight 59 tonsLoaded front end loader weight 74 tonsAverage front end loader weight 66 tonsHourly trips 1 trips/hour Assuming 1 trip per hourAnnual trips 218 trips/yearHourly travelled distance 0.189 VMT/hourAnnual travelled distance 42 VMT/yearSilt content 3.4 wt. % AP-42; Table 13.2.4-1, Taconite Mining and Processing (Pellets); 11/06Days with >0.01" precipitation 120 days/yr AP-42; Figure 13.2.1-2; 1/11 for Toledo, OhioUnpaved road chemical stablization control efficiency 95% Ohio EPA RACM Guidance Table 2.1.1-3

Unpaved road traffic uncontrolled emission factorsHourly (lb/VMT) Annual (lb/VMT)

PM 8.16 5.48PM10 1.94 1.30PM2.5 0.19 0.13AP-42, Page 13.2.2-4 (11/2006)

Potential to Emit:Pollutant Controlled

Feed Stockpile FEL Fugitive (lb/hour)

Emissions (tons/year)

PM 0.08 0.01PM10 0.02 0.00PM2.5 0.002 0.00

Annual average distance traveled by the front end loader = 500 feet one way in the storage area (mix of paved and unpaved surface)

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Table C-56: Feed Recovery Transfer from FEL to Hopper

Emission Unit: TR-30, Feed Recovery from FEL to HopperGAD Point 97

Parameters:Feed transfer rate 15 tons/hour

3,210 tons/yearExpected operation 273 hours/year Assuming 80% hourly operating rateNumber of drop points 1U = mean windspeed for Toledo 9.40 mph AP-42, Table 7.1-9, 11/2006M = moisture content 1.5 % Assumed worst case moisture content

Feed drop point uncontrolled emission factorsPM 0.008 lb/tonPM10 0.0038 lb/tonPM2.5 0.00058 lb/tonAP-42, Page 13.2.4-3 (11/2006)

Potential to Emit:Pollutant Feed Drop

(lb/hour)Total Emissions (tons/year)

PM 0.12 0.01PM10 0.06 0.01PM2.5 0.008 0.00

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Table C-57: Front End Loader Reclaim Fugitive Emissions (Cheminal stablization)

Emission Unit: FEL-6, Front End Loader Fugitive Emissions from Product Oversize ReclaimGAD Point 98

Parameters:Product Oversize Stockpile Reclaim by Front End Loade 15 tons/hour 1 trips per hour

6,419 tons/yearExpected operation 546 hours/year

Front end loader travel distance 0.19 milesEmpty front end loader weight 59 tonsLoaded front end loader weight 74 tonsAverage front end loader weight 66 tonsHourly trips 1 trips/hour Assuming 1 trip per hourAnnual trips 437 trips/yearHourly travelled distance 0.189 VMT/hourAnnual travelled distance 83 VMT/yearSilt content 3.4 wt. % AP-42; Table 13.2.4-1, Taconite Mining and Processing (Pellets); 11/06Days with >0.01" precipitation 120 days/yr AP-42; Figure 13.2.1-2; 1/11 for Toledo, OhioUnpaved road chemical stablization control efficiency 95% Ohio EPA RACM Guidance Table 2.1.1-3

Unpaved road traffic uncontrolled emission factorsHourly (lb/VMT) Annual (lb/VMT)

PM 8.16 5.48PM10 1.94 1.30PM2.5 0.19 0.13AP-42, Page 13.2.2-4 (11/2006)

Potential to Emit:Pollutant Controlled

Oversized Stockpile FEL Fugitive (lb/hour)

Emissions (tons/year)

PM 0.08 0.01PM10 0.02 0.00PM2.5 0.002 0.00

Annual average distance traveled by the front end loader = 500 feet one way in the storage area (mix of paved and unpaved surface)

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Table C-58: Product Oversize Transfer from FEL to Hopper

Emission Unit: TR-31, Product Oversize from FEL to HopperGAD Point 99

Parameters:Product Oversize transfer rate 15 tons/hour

6,419 tons/yearExpected operation 546 hours/year Assuming 80% hourly operating rateNumber of drop points 1U = mean windspeed for Toledo 9.40 mph AP-42, Table 7.1-9, 11/2006M = moisture content 1.5 % Assumed worst case moisture content

Product Oversize drop point uncontrolled emission factorsPM 0.008 lb/tonPM10 0.0038 lb/tonPM2.5 0.00058 lb/tonAP-42, Page 13.2.4-3 (11/2006)

Potential to Emit:Pollutant Product Oversize

(lb/hour)Total Emissions (tons/year)

PM 0.12 0.03PM10 0.06 0.01PM2.5 0.008 0.00

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Table C-59: Admin Building Emergency Generator

Emission Unit: P-10, Emergency Diesel Generator 133 bhpGAD Point 92

Parameters:Expected operation 500 hours/yearPower Output 133 bhp Standby rating

99 kWFuel Use Rate 6.9 gal/hourDiesel heating value 138000 Btu/gallon 40 CFR Part 98 Table C-1Heat Input Rate 0.95 MMBtu/hourPM 0.3 g/kW-hr Filterable only from NSPS IIII and 40 CFR 89.112(a) Tier 2PM10 0.33 g/kW-hr Filterable from PM and Condensable from AP-42PM2.5 0.33 g/kW-hr Same as PM10NOx 4.0 g/kW-hr NSPS Subpart IIII and 40 CFR 89.112(a) Tier 3 (assumed no NMSO2 0.007 g/kW-hr Assuming 15 ppm sulfur fuelCO 5.0 g/kW-hr NSPS Subpart IIII and 40 CFR 89.112(a) Tier 3VOC 0.0006 lb/hp-hr AP-42 Table 3.4-1CO2 163.05 lb/MMBtu 40 CFR Part 98 Table A-1 and C-1 and C-2CO2e 163.61 lb/MMBtu 40 CFR Part 98 Table A-1 and C-1 and C-2PM condensable 0.0077 lb/MMBtu AP-42 Table 3.4-2

Potential to Emit:Pollutant RICE Exhaust

(lb/hour)Emissions (tons/year)

PM 0.07 0.02PM10 0.07 0.02PM2.5 0.07 0.02NOx 0.87 0.22SO2 0.00 0.00CO 1.09 0.27VOC 0.09 0.02CO2 155 39CO2e 156 39

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Table C-60: Wastewater Treatment Sludge Truck Transport Fugitive Emissions (Watering & sweeping)

Emission Unit: HR-5, Truck Transport Fugitive Emissions from Wastewater Treatment SludgesCH2M GAD Points 100

Parameters:Sludge transfer by truck 24 tons/hour Assuming max of 336 days for 24-hour or at least 1 trip per hour

142,040 tons/yearTruck travel distance 0.73 milesEmpty truck weight 15 tons Assumed 30,000 lbLoaded truck weight 39 tons Assumed 78,000 lbAverage truck weight 27 tonsSludge weight per load 24 tonsHourly trips 1 trips/hourAnnual trips 5,918 trips/yearHourly travelled distance 0.7 VMT/hourAnnual travelled distance 4,321 VMT/yearPaved road silt loading 9.7 g/m2 AP-42; Table 13.2.1-3; 1/11 for Iron and Steel ProductionDays with >0.01" precipitation 120 days/yr AP-42; Figure 13.2.1-2; 1/11 for Toledo, OhioTime between watering application for paved roads 2 hours - apply water flushing followed by sweeping (weather permitting) at 2.2 l/m2

Control efficiency for measures 95%

Paved road traffic uncontrolled emission factorsHourly (lb/VMT) Annual (lb/VMT)

PM 2.51 2.30PM10 0.50 0.46PM2.5 0.12 0.11AP-42, Page 13.2.1-4 (1/2011)

Potential to Emit:Pollutant Controlled

Sludge Truck Fugitive (lb/hour)

Emissions (tons/year)

PM 0.08 0.23PM10 0.02 0.05PM2.5 0.004 0.01

Annual average round trip travel distance for trucks

Control of Open Fugitive Dust Sources EPA-450/3-88-008, Table 2-4 (96-0.263V)%, V = No. of Vehicles since application

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Midwest Terminals of Toledo, Inc.

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Table M-1: Iron Oxide Transfer from Boat to Midwest Hopper to Conveyor to Stacker

Emission Unit: MTR-1, MTR-2, MTR-3 Transfer Point Oxide Boat Unloading to Hopper to Conveyor to StackerCH2M GAD Points 13, 14, 15 Existing operations no short term increase

Parameters:Oxide transfer rate from boat 3,970 tons/hour

3,594,666 tons/yearExpected operation 1,200 hours/year Based on 80% hourly operating rateNumber of controlled drop points 3 From boat -> hopper, hopper -> conveyor, conveyor -> stackerU = mean windspeed for Toledo 9.40 mph AP-42, Table 7.1-9, 11/2006M = moisture content 2.5 % Source: Pellet Boat Moisture from Northshore Data (2009-2014Water or chemical sprays control eff. 95% Ohio EPA RACM Guidance Table 2.1.3-3

Source: Ohio EPA RACM Plan

Oxide drop point uncontrolled emission factorsPM 0.004 lb/tonPM10 0.002 lb/tonPM2.5 0.0003 lb/tonAP-42, Page 13.2.4-3 (11/2006)

Potential to Emit:Pollutant Total Emissions

(tons/year)PM 1.06PM10 0.50PM2.5 0.08

Short term emissions will not increase

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Table M-2: Iron Oxide Transfer from Stacker to Hopper

Emission Unit: MTR-4 Transfer Point Oxide Stacker to HopperCH2M GAD Point 16 Existing operations no short term increase

Parameters:Oxide transfer rate from boat 3,970 tons/hour

3,594,666 tons/yearExpected operation 1,200 hours/year Based on 80% hourly operating rateNumber of controlled drop points 1 From Stacker -> hopperU = mean wind speed for Enclosure 1 mph Windshield around the hopper to reduce wind effectM = moisture content 2.5 %Control efficiency 70% Ohio EPA RACM Guidance OAC 3745-17-08 Page 2-61

Source: Ohio EPA RACM Plan

Oxide drop point uncontrolled emission factorsPM 0.00021 lb/tonPM10 0.00010 lb/tonPM2.5 0.00002 lb/tonAP-42, Page 13.2.4-3 (11/2006)

Potential to Emit:Pollutant Total Emissions

(tons/year)PM 0.12PM10 0.05PM2.5 0.01

Short term emissions will not increase

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Appendix C – BACT Impact Analysis Tables

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Appendix C

Annualized Capital Costs (1992 $)Monitoring Equipment = $1,495

Rupture Disks & Assemblies = $36,342Initial Leak Repairs = $0

Annual Operating Costs (1992 $)Maintenance Charges =

Monitoring Instrument = $4,280Rupture Disks & Assemblies = $10,395

Miscellaneous Charges =Monitoring Instrument = $260

Rupture Disks & Assemblies = $8,478Labor Charges =

LDAR Monitoring = $12,940Subsequent Repairs = 13179.7

Administrative Support = $8,124Cost‐Effectiveness Summary

Annualized Costs in 1992 $ = $95,494June 1992 CPI = 419.900May 2019 CPI = 767.138

Annualized Costs in 2019 $ = $174,463NG Recovered (T/yr) = 103.4VOC Controlled (T/yr) = 2.86

Recovery Credit @ $3.47/MMBtu = $17,316VOC Control Cost Credit @ $20,000/T = $57,279

Net Annualized Cost in 2019 $ = $99,867Net CH4 Reductions as CO2e (T/yr)= = 2,584.8Net Cost‐Effectiveness ($/T CO2e) = $39 = (Net Annualized Cost in 2019 $) / (Net CH4 Reductions as CO2e (T/yr)=)

Cost Data from: Hazardous Air Pollutant Emissions from Process Units in the Synthetic Organic Chemical Manufacturing Industry‐Background 

Based on weighted avg. LDAR efficiency of 93.7%.Based on weighted avg. LDAR efficiency of 93.7%.Based on 103.4 T/yr of CH4 recovered.Assumes that a control cost of $20,000 per ton of VOC is unreasonable.= (Annualized Costs in 2019 $) ‐ (Recovery Credit @ $3.47/MMBtu)Based on CH4 GWP.

(Annualized Costs in 1992$) x May 2019 CPI) / (June 1992 CPI)

HON BID, Table 6‐12; adjusted for Component Count.

HON BID, Table 6‐12.HON BID, Table 6‐12; adjusted for Component Count.

HON BID, Table 6‐12; assumed miminum cost to operate program.HON BID, Table 6‐12; adjusted for Component Count.HON BID, Table 6‐12; assumed miminum cost to operate program.

Sum of above values.From: http://www.economagic.com/em‐cgi/data.exe/blscu/CUUR0000AA0From: http://www.economagic.com/em‐cgi/data.exe/blscu/CUUR0000AA0

HON BID, Table 6‐12.

Table C.     Natural Gas Equipment Components LDAR Program Cost Estimate

HON BID, Table 6‐12.HON BID, Table 6‐12; adjusted for Component Count.No initial leaks assumed at new construction.

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Appendix D – Air Dispersion Modeling Report

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APPENDIX D

AIR DISPERSION MODELING FOR THE PROPOSED IRONUNITS LLC

HOT BRIQUETTED IRON PRODUCTION FACILITY IN TOLEDO, OHIO

Prepared for: IronUnits LLC

200 Public Square, Suite 3000 Cleveland, OH 44114

Prepared by: RTP Environmental Associates

304A West Millbrook Road Raleigh, North Carolina 27609

Original Submittal September 2017 Revised September 2019

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Table of Contents 1.0 INTRODUCTION ................................................................................................. 1-1 2.0 PROJECT DESCRIPTION .................................................................................. 2-1 3.0 SITE DESCRIPTION ........................................................................................... 3-1 4.0 MODEL SELECTION AND MODEL INPUT ........................................................ 4-1

4.1 Model Selection ................................................................................................ 4-1 4.2 Model Control Options and Land Use .............................................................. 4-1 4.3 Source Data ..................................................................................................... 4-2 4.4 Ambient Monitoring and Monitored Background Data ...................................... 4-8 4.5 Receptor Data ................................................................................................ 4-14 4.6 Meteorological Data ....................................................................................... 4-15

5.0 MODELING METHODOLOGY ............................................................................ 5-1 5.1 Pollutants Subject to Review ............................................................................ 5-1 5.2 Significant Impact Analysis ............................................................................... 5-1 5.3 Preconstruction Monitoring ............................................................................... 5-2 5.4 NAAQS Analysis .............................................................................................. 5-3 5.5 PSD Increment Analysis ................................................................................... 5-5 5.6 NO2 Analyses ................................................................................................... 5-6 5.7 Secondary PM2.5 Analyses ............................................................................. 5-8 5.8 Ozone Analyses ............................................................................................... 5-9

6.0 MODEL RESULTS .............................................................................................. 6-1 6.1 Significant Impact Analysis Results .................................................................. 6-1 6.2 1-hr NO2 Increment and Air Toxics Analysis Results ....................................... 6-1 6.3 NAAQS Analysis Results ................................................................................. 6-2 6.4 Increment Analysis Results .............................................................................. 6-2 6.5 Secondary PM2.5 Analysis Results .................................................................. 6-4 6.6 Ozone Analysis Results ................................................................................... 6-4 6.7 Model Input and Output Files ........................................................................... 6-4

7.0 CLASS II VISIBILITY ANALYSIS ........................................................................ 7-1 8.0 CLASS I AREA IMPACTS ................................................................................... 8-1

8.1 Class I AQRV Analysis ..................................................................................... 8-1 8.2 Class I Increment Analysis ............................................................................... 8-1

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List of Tables

Table 1. Background Concentrations 2015-2017 ...................................................... 4-13 Table 2. Receptor Grid Spacing ................................................................................ 4-15 Table 3. PSD Class II Significant Impact Levels ......................................................... 5-2 Table 4. PSD Preconstruction Monitoring Exemption Levels ...................................... 5-3 Table 5. Monitored and Modeled Values Used to Assess NAAQS Compliance .......... 5-5 Table 6. National Ambient Air Quality Standards ........................................................ 5-5 Table 7. PSD Increments ............................................................................................ 5-6 Table 8. Class II Significant Impact Analysis Results .................................................. 6-1 Table 9. State 1-hr NO2 Increment and Air Toxics Analysis Resultsa ......................... 6-2 Table 10. NAAQS Analysis Results............................................................................. 6-3 Table 11. PSD Increment Analysis Results ................................................................. 6-5 Table 12. Hypothetical Source Data and Calculated HBI Secondary PM2.5 Impacts . 6-8 Table 13. Hypothetical Source Data and Calculated Ozone Impacts .......................... 6-9 Table 12. Level-1 Class II Visibility Analysis Results................................................... 7-3

List of Figures Figure 1. General Location of the IronUnits Facility .................................................... 3-2 Figure 2. Specific Location of the IronUnits Facility ..................................................... 3-3 Figure 3. Land Use within Three Kilometers ............................................................... 4-3 Figure 4. HBI Facility Plot Plan .................................................................................... 4-6 Figure 5. HBI Facility Three Dimensional Plot Plan (View from SE) ............................ 4-7 Figure 6. Ambient Air Quality Monitors within 100km of the IronUnits Site ................ 4-10 Figure 7. Ambient Air Quality Monitors Used in the Source Impacts Analysis ........... 4-11 Figure 8. HBI Facility Near-field Receptor Grid ......................................................... 4-16 Figure 9. Metcalf Field Location Relative to HBI Facility ........................................... 4-17 Figure 10. Metcalf Field (KTDZ) Windrose 2014-2017. ............................................. 4-18 Figure 11. PM2.5 24-Hour 50% Increment Exceedence Locations ............................. 6-6 Figure 12. PM10 24-Hour 50% Increment Exceedence Locations .............................. 6-7 Figure 13. Class I Areas Located within Three Hundred Kilometers ........................... 8-2

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1-1

1.0 INTRODUCTION This document presents the results of the air quality dispersion modeling analysis

conducted for the proposed Iron Units LLC (“IU”) Hot Briquetted Iron (“HBI”) production

facility that is under construction in Toledo, Ohio. This analysis was originally

conducted in 2017 as part of the initial air quality permitting efforts for the facility. The

initial permitting and models were based upon preliminary facility design specifications.

Final engineering designs for the project have advanced and the technology provider for

the Core Plant, MIDREX, has updated its emission estimates to more accurately

characterize CO emissions rates throughout the process based on recent stack test

data collected from other facilities and improvements to its emission estimating model.

The air quality modeling analysis has therefore been revised to address these project

updates. The primary revisions to the modeling conducted in 2017 involve: updating the

meteorological and background ambient air quality data, updating the facility plot plan to

include minor new structures, revised stack parameter for several sources, refined the

layout of the furnace tower, slight changes to the truck hauling routes, relocation and

addition of several emission units, and refined emissions estimates for several sources.

With the facility design changes incorporated, the ultimate conclusion of the initial

dispersion modeling analysis is not affected. The current modeling evaluation continues

to demonstrate compliance with all applicable air quality standards.

The analysis evaluated emissions of the criteria pollutants regulated under the

applicable provisions of the Prevention of Significant Deterioration (“PSD”) regulations

of Ohio Administrative Code (“OAC”) Chapter 3745-31. The criteria pollutant analysis

was conducted to ensure that the proposed project will not cause or contribute to air

pollution in violation of a National Ambient Air Quality Standard (NAAQS) or increment

for all criteria pollutants proposed to be emitted in excess of the PSD significant

emission rates (“SERs”).

Consistent with Ohio EPA Air Toxics Policy1 and Ohio Environmental Protection

Agency’s (“OEPA”) Engineering Guide 692, toxic air pollutants emitted in quantities of

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one ton per year or greater were also evaluated. Only the hexane emissions from the

Project’s use of natural gas and ammonia from the degasser exhaust and cooling tower

are estimated to potentially exceed this threshold. Model results were compared to the

appropriate one-hour Maximum Acceptable Ground-Level Concentrations (“MAGLC”) or

acceptable incremental impacts.

The current analysis followed the modeling protocol submitted to and approved by the

OEPA (with revisions), the modeling procedures outlined in the Environmental

Protection Agency’s Guideline on Air Quality Models3 (Guideline or Appendix W), the

Engineering Guide 69,), and associated EPA modeling policy and guidance.

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2.0 PROJECT DESCRIPTION IronUnits LLC (“IU”) is constructing a Hot Briquetted Iron (HBI)/ Direct Reduced Iron

(DRI) manufacturing facility in Toledo, Lucas County, Ohio identified as the “Project”.

The Project will utilize the MIDREX process to produce up to 2.48 million short tons per

year of HBI or DRI from low-silica taconite pellets. The Project is situated on a

brownfield parcel known as Ironville located on the southwest corner of Millard Ave and

Front Street. The Project will use lake vessels, trains, and trucks to transport various

raw-materials and products to and from the site.

The Project will result in increases in emissions of nitrogen oxides (“NOx”), particulate

matter (“PM”) with an aerodynamic diameter of less than 10 microns (“PM10”), PM with

an aerodynamic diameter of less than 2.5 microns (“PM2.5”), and carbon monoxide

(“CO”) that are in excess of PSD Significant Emission Rates (“SERs”).

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3.0 SITE DESCRIPTION The Project occupies approximately 130 acres on a former industrial site known as

Ironville, a brownfield parcel. The approximate Universal Transverse Mercator (UTM)

coordinates of the HBI Facility are 293,680 meters east and 4,616,450 meters north

(UTM Zone 17, NAD 83). Figure 1 shows the general location of the HBI Facility.

Figure 2 shows the specific HBI Facility location on a 7.5-minute U.S. Geological Survey

(USGS) topographic map.

The Project is classified under the regulations governing PSD (OAC 3745-31-11

through 20) as a new major source. Lucas County is classified as attainment or

unclassifiable for all regulated pollutants.

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Figure 1. General Location of the IronUnits Facility

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Figure 2. Specific Location of the IronUnits Facility

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4.0 MODEL SELECTION AND MODEL INPUT 4.1 Model Selection The latest version of the AMS/EPA Regulatory Model (AERMOD, Version 18081) was

used to conduct the dispersion modeling analysis. AERMOD is a Gaussian plume

dispersion model that is based on planetary boundary layer principals for characterizing

atmospheric stability. The model evaluates the non-Gaussian vertical behavior of

plumes during convective conditions with the probability density function and the

superposition of several Gaussian plumes. AERMOD is a modeling system with three

components: AERMAP is the terrain preprocessor program, AERMET is the

meteorological data preprocessor and AERMOD includes the dispersion modeling

algorithms.

AERMOD is the required default model for calculating ambient concentrations near the

HBI Facility based on the model's ability to incorporate multiple sources and source

types. The model can also account for convective updrafts and downdrafts and

meteorological data throughout the plume depth. The model also provides parameters

required for use with up to date planetary boundary layer parameterization. The model

also has the ability to incorporate building wake effects and to calculate concentrations

within the cavity recirculation zone. All model options were selected as recommended

in the EPA Guideline on Air Quality Models.

Oris Solution's BEEST Graphical User Interface (GUI) was used to run AERMOD. The

GUI uses an altered version of the AERMOD code to allow for flexibility in the file

naming convention. The dispersion algorithms of AERMOD are not altered. Therefore,

a model equivalency evaluation pursuant to Section 3.2 of 40 CFR 51, Appendix W is

not warranted.

4.2 Model Control Options and Land Use AERMOD was run in the regulatory default mode for all pollutants. The NO2 modeling

included the Plume Volume Molar Ratio Method (PVMRM) in the NAAQS analysis. This

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option is discussed in more detail in Section 5.7 of this protocol. The default rural

dispersion coefficients in the model were used. This is supported by the Land Use

Procedure consistent with subsection 7.2.3(c) of the Guideline and Section 5.1 of the

AERMOD Implementation Guide.

In assessing land use, the USGS 2006 National Land Cover Data (NLCD) within 3km of

the site were converted to Auer 1978 land use types, using recommendations from the

Pennsylvania Department of Environmental Protection, and evaluated.4 It was

determined that the land use in the vicinity of the Project is predominantly rural (less

than 30% of the area is classified as urban - Figure 3). Only the red and dark red

regions in the figure (NLCD categories 23 and 24) are classified as urban.

4.3 Source Data Source Characterization Point Sources Most emission sources at the Project site vent to stacks with a well defined opening.

These sources were modeled as point sources in AERMOD. Several other types of

sources such as fugitive emissions also required evaluation.

Fugitive Emissions Fugitive emissions are those that are not emitted from a well defined opening. These

were modeled as volume sources. The initial dispersion coefficients (sigma y and

sigma z) were calculated based upon the dimensions of the area of release and the

equations contained in Table 3-1 of the AERMOD User’s Guide.

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Figure 3. Land Use within Three Kilometers (Three Kilometer Radius Shown As Blue Circle)

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Haul roads were modeled pursuant to procedures adopted by the EPA Haul Road

Workgroup5 as outlined in the five steps below:

Step 1: The adjusted width of the “road” was calculated as the actual road width plus 6 meters. The additional width represents turbulence caused by the vehicle as it moves along the road. Step 2: The height of the volume was set to 1.7 times the height of the vehicle generating the emissions. Step 3: The initial horizontal sigma for each volume was calculated by dividing the adjusted width by 2.15. Step 4: The initial vertical sigma was calculated by dividing the height of the volume determined in Step 2 by 2.15. Step 5: The release point height was calculated as the height of the volume divided by two. This point is in the center of the volume.

Flare There will also be a flare at the facility that will be used in event of process

upsets/malfunctions and also during facility startups and shutdowns.

Upsets/malfunctions are not considered to be normal operations and are not included in

establishing emission limits per the Guideline. Therefore, only emissions associated

with the startups and shutdowns and the pilot flame on the flare were modeled. The

startup and shutdown events were modeled pursuant to OEPA guidance. The effective

stack height (H, in meters) was computed based on the actual height of the flare (98.4ft)

and the heat release rate (Q) (1677 MMBtu/hr) according to the following equation:

Hequivalent = Hactual + 0.944(Q)0.478, or 131.2ft The effective flare diameter (d, in meters) was computed as a function of heat release

rate, Q, and the following equation:

dequivalent = 0.1755(Q)0.5

An exit temperature of 1273°K and velocity of 20 m/sec was assumed.

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As there is minimal heat release and associated buoyancy associated with the pilot,

actual stack height and diameter were modeled during the periods when the flare is not

used and the pilot remains lit.

Good Engineering Practice Stack Height Analysis A Good Engineering Practice (GEP) stack height evaluation was conducted to

determine appropriate building dimensions to include in the model and to calculate the

GEP formula stack height used to justify stack height credit for stacks to be constructed

in excess of 65m. Procedures used were in accordance with those described in the

EPA Guidelines for Determination of Good Engineering Practice Stack Height

(Technical Support Document for the Stack Height Regulations-Revised)6. GEP

formula stack height, as defined in 40 CFR 51, is expressed as GEP = Hb + 1.5L, where

Hb is the building height and L is the lesser of the building height or maximum projected

width. Building/structure locations were determined from a facility plot plan. The

structure locations and heights were input to the EPA’s Building Profile Input Program

(BPIP-PRIME) computer program to calculate the direction-specific building dimensions

needed for AERMOD. The HBI Facility plot plan is shown in Figure 4. A three

dimensional rendering of the facility is shown in Figure 5. All stacks and structures were

included in the BPIP runs.

All model input data, including the fugitive sigma y and z calculations, are provided in

Attachment A to this report.

Source Groupings and Modeled Pollutant Names The Project will result in significant emission increases for NO2, CO, PM10 and PM2.5.

Two pollutants were modeled for NO2. “NOx” was modeled for annual emissions and

“NO2” was modeled for short-term (1-hr) emissions. Likewise, “PM-10” was modeled

for annual PM10 emissions and “PM10” (without the hyphen) was modeled for 24-hr

emissions. The same naming convention was used for PM2.5 emissions. “PM-25”

represents annual emissions and “PM25” represents 24-hr emissions.

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Figure 4. HBI Facility Plot Plan

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Figure 5. HBI Facility Three Dimensional Plot Plan (View from SE)

Three source groupings were used in the NAAQS demonstration. The “ALL” group

consisted of all emission sources, including the HBI sources. The source group called

“CLIFFS” was used to determine only the impacts of the proposed HBI sources and was

used in the NAAQS culpability analyses. A group called “LT20K” was used in the

PM2.5 annual NAAQS analysis to represent the nearby emission sources located within

20km of the HBI site.

Four source groups were used in the PSD increment analyses. The group called

“PM10INC” was used for all sources that consume PM10 increment. Model results for

this group were compared to the PM10 increments. A group called “PM25INC” was

used for all sources that consume PM2.5 increment. Model results for this group were

compared to the PM2.5 increments. All sources were conservatively assumed to

consume NO2 increment, so the “ALL” source group was used in this assessment. The

source group called “CLIFFS” was used to determine only the impacts of the proposed

HBI sources and was used in the increment culpability analyses.

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4.4 Ambient Monitoring and Monitored Background Data

Ambient, background pollutant concentrations from sources not directly modeled are

needed to establish a representative background concentration to complete the NAAQS

portion of the Source Impact Analysis of OAC 3745-31-16. The background

concentrations are added to the modeled concentrations to assess NAAQS compliance.

Ambient pollutant concentrations are also needed to fulfill the Air Quality Analysis

requirement of OAC 3745-31-14. Air quality data needed to satisfy this requirement are

required for each pollutant proposed to be emitted in significant amounts. For the

proposed HBI Facility, these pollutants include: NO2, CO, PM10, PM2.5 and NOx as

(ozone precursor).a

Pursuant to OAC 3745-31-13(H), pollutants with projected increases in ambient

concentrations due to the project below the Significant Monitoring Concentrations

(SMC) are exempt from the pre-application monitoring requirement under OAC 3745-

31-14. As shown in Section 6, the HBI Facility would qualify for such exemptions with

respect to all listed pollutants except for PM10, PM2.5, and CO because the maximum

modeled impacts are less than the SMC. However, in light of the decision of the D.C.

Circuit Court of Appeals Sierra Club v. EPA,7 out of abundance of caution, IU has

elected not to rely on the exemption. IU has elected to use existing ambient monitoring

data in lieu of preconstruction monitoring data consistent with USEPA guidance on this

issue.

The EPA's Ambient Monitoring Guidelines8, other EPA interpretive guidance, and EPA

administrative decisions clarify that representative, existing air quality monitoring data

may be used to fulfill the PSD pre-construction monitoring requirements and establish

the background concentrations needed for assessing NAAQS compliance, in lieu of

monitoring data from the precise area in the vicinity of the proposed source or

modification. EPA’s Monitoring Guidelines suggest specific criteria to determine

a Since the HBI Facility will result in an emissions increase of 100 tons per year of volatile organic compounds or NOx, it is also required to gather ambient ozone air quality data (exemption under OAC 3745-31-13(H)(1)(f)).

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representativeness of off-site data: quality of the data, currentness of the data, and

monitor location.

As shown in Figure 6, there are numerous air quality monitors within 100km of the

proposed HBI Facility which can be used to satisfy the requirements for ambient

monitoring data. Existing monitoring data were evaluated in relation to the criteria

provided in EPA’s Ambient Monitoring Guidelines9 as being representative of the IU site

and proposed for use in both the Source Impact Analysis of OAC 3745-31-16 and the

Air Quality Analysis requirements of OAC 3745-31-14.

RTP has used the 2015-2017, quality assured ozone data from the Erie monitor in

Toledo (AQS # 39-095-0024) to establish representative background ozone

concentrations to fulfill the OAC 3745-31-14 requirements. This monitor ceased

operation in September of 2018, so the 2018 data were not employed. For reasons

discussed in Section 5.6 below, hourly data from the ozone monitor in Allen Park,

Michigan (AQS # 26-163-0001) were used in conducting the 1-hr NO2 analysis

pursuant to OAC 3745-31-16. The Allen Park monitor was also used to establish CO

concentrations.

There are three PM2.5 ambient monitors in the vicinity (within 15km) of the proposed

site (Figure 7). The Toledo Water Filtration monitor (AQS #39-095-0028) is located

about 1.1km south of the site. The next closest monitor is the Erie site (AQS #39-095-

0024) at 6.4km west-southwest. The RAPs site (AQS #39-095-0026) is 14.8km to the

west-southwest. The Toledo Water Filtration monitor was used to establish background

values as required by OAC 3745-31-14. However, Toledo is a highly industrialized area

and each of the PM2.5 monitors within 15km of the proposed site is heavily influenced

by the local industry and, therefore, not representative of background PM2.5

concentrations independent of the sources specifically modeled in the vicinity.

Considering that the modeled inventory of offsite PM2.5 sources was quite extensive

(there are in excess of 400 individual offsite emission sources in the NAAQS model),

there is the potential of “double counting” sources in both the model and monitored

background values. In addition, according to the EPA’s 2014 Guidance for PM2.5

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Figure 6. Ambient Air Quality Monitors within 100km of the IronUnits Site

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Figure 7. Ambient Air Quality Monitors Used in the Source Impacts Analysis (Monitors Circled)

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Permit Modeling, greater emphasis is generally placed on the monitored background

contribution of secondary particulate contributions relative to the modeled inventory for

PM2.5. Furthermore, monitored background PM2.5 concentrations are likely to be more

homogenous across the modeling domain than other pollutants. Use of a monitor that

is not influenced by the localized industry in Toledo yields a better representation of the

secondary formation. The use of a more rural monitor is therefore appropriate. We

therefore used the most recent available, quality assured data (2015-2017) from the

PM2.5 monitor in Monroe Co., Michigan (AQS Site #26-115-0006) to establish the

background values required pursuant to OAC 3745-31-16.

There are no PM10 or NO2 monitors in the immediate vicinity. We relied on the PM10

monitor at the Barr School near Lorain (AQS Site #39-093-3002), and the NO2 monitor,

near Cleveland, at Cleveland Near Road (AQS Site #39-035-0073) to establish

representative background concentrations to fulfill both the OAC 3745-31-14 and 16

requirements.

A range of monitored background NO2 values that consider seasonal and diurnal

variation was used to assess compliance with the 1-hr NAAQS. These seasonal values

reflect the three year average (2015-2017) of the 98th percentile value by hour of day

and by season. These seasonal NO2 values were added to the modeled value within

AERMOD.

The background values are provided in Tables 1 and 2. The existing monitoring data

satisfy the criteria provided in the Ambient Monitoring Guidelines as being

representative of the IUs site.

The existing monitoring data also satisfy the criteria for location, data quality and

currentness, provided in EPA’s Ambient Monitoring Guidelines as being representative

of the site.

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Table 1. Background Concentrations 2015-2017

Pollutant Averaging

Time Design Value (ppb)[µg/m3] Basis Monitor Site Location

NO2 1-hour (40.7) [76.9] Avg 98% Cleveland Near Road (AQS #39-035-0073) Annual (9.35) [17.7] Avg

CO 1-hour (2400) [2743] Max Allen Park (AQS #26-163-0001) 8-hour (1630) [1863] Max

Ozone 8-hour (67) Avg Erie (AQS #39-095-0024)

PM10 24-hour [35.0] Max Barr School (AQS #39-093-3002)

PM25 24-hour [21.5] Avg 98% Toledo Water Filtration (AQS #39-095-0028) Annual [8.22] Avg

24-hour [21.5] Avg 98% State Park Road

(AQS #26-115-0006) Annual [8.22] Avg

Notes: “Avg 98%” is the 3-yr average of the 98% daily maximum values. “Max H2H” is the maximum of the highest second high values over the three years. Ozone values are from 2013-15 (see the February 25, 2016, Area Designation Memo from Janet McCabe to the Regional Administrators.

Table 2. Cleveland 98% Hourly NO2 (ppb) By Season and Hour of Day Model Ending

Hour Winter Spring Summer Fall01 37.67 39.33 17.33 22.0002 39.33 37.33 17.33 23.0003 39.33 38.67 18.00 24.0004 41.67 38.00 18.00 28.0005 39.33 36.00 21.00 28.3306 40.33 39.67 26.33 32.0007 39.00 41.00 27.33 34.3308 38.00 38.33 25.33 35.0009 36.33 26.67 23.00 34.3310 29.67 26.00 19.33 25.6711 27.00 26.00 17.67 22.0012 23.00 19.00 17.33 19.6713 21.00 19.33 18.00 19.0014 22.33 19.00 18.67 20.3315 24.67 20.67 19.67 22.3316 25.00 23.33 18.00 23.6717 29.00 27.67 18.33 24.0018 30.33 29.00 17.00 24.6719 30.67 26.00 17.33 28.3320 31.67 31.00 17.67 27.3321 37.00 29.00 19.67 26.6722 36.33 28.33 15.67 25.6723 36.33 34.67 16.67 26.0024 38.00 36.67 15.67 26.33

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Monitor Location Of the monitors available, these monitors represent background concentrations as they

are the closest monitors with data for the pollutants of concern that are not also

significantly influenced by the localized source impacts.

Data Quality The monior data were collected and quality assured by the MDEQ for the Monroe and

Allen Park monitors and OEPA for the other monitors.

Currentness of Data The data were collected during 2015-2017, which represents the most recent quality

assured data available for use in assessing compliance.

4.5 Receptor Data Modeled receptors were placed in all areas considered as "ambient air" pursuant to 40

CFR 50.1(e). Ambient air is defined as that portion of the atmosphere, external to

buildings, to which the general public has access. Approximately 8,400 receptors were

used in the AERMOD significant impacts analysis. The receptor grid consists of four

cartesian grids and receptors spaced at 25m intervals along the facility fenceline. The

first cartesian grid extends approximately 1km from the fence in all directions.

Receptors in this region are spaced at 50m intervals. The second grid extends to

2.5km. Receptor spacing in this region is 100m. The third grid extends to 7.5km with a

spacing of 500m. The fourth grid extends to 15km with a receptor spacing of 1,000m.

The receptor grid was designed such that maximum facility impacts fall within the 50m

spacing of receptors. The receptor grid spacing is presented in Table 3.

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Table 3. Receptor Grid Spacing

Receptor Spacing (m)Distance from Facility

Fence (m)50 1,000

100 2,500500 7,500

1,000 15,000 The HBI Facility is located in northeastern Ohio. Terrain within 10km of the site is

generally flat. Receptor elevations and hill height scale factors were calculated with

AERMAP (18081). The elevation data were obtained from the USGS 1/3 arc second

National Elevation Data (NED) obtained from the USGS. Locations were based upon a

NAD83, UTM Zone 17 projection. The near-field receptor grid is presented in Figure 8.

4.6 Meteorological Data

The 2013-2017, 5-year sequential hourly surface meteorological data collected at the

Metcalf Field (KTDZ, WBAN 04848) and upper air data from the Detroit Michigan Airport

(KDTX, WBAN 04830) were used in the analysis. These data were processed by

OEPA using AERMET version 18081 and AERMINUTE version 15272. OEPA used the

surface friction velocity asjustment (adj u*) in processing the data. Data completeness

criteria were evaluated by OEPA, and each year of meteorological data exceeds 90%

completeness. Meteorological data from these years, 2013-2017 from both the surface

and upper air stations have been thoroughly vetted for several modeling applications

conducted for the State of Ohio.

KTDZ is located approximately 12km to the south as shown in Figure 9. The 2013-2017

windrose is provided in Figure 10.

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Figure 8. HBI Facility Near-field Receptor Grid

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Figure 9. Metcalf Field Location Relative to HBI Facility

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Figure 10. Metcalf Field (KTDZ) Windrose 2014-2017.

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5.0 MODELING METHODOLOGY

5.1 Pollutants Subject to Review

Only the criteria pollutants whose emissions increases exceed the PSD significance

thresholds and are therefore subject to PSD review were evaluated in the modeling

analysis. These pollutants include CO, NO2, PM10 and PM2.5. NOx as an ozone

precursor was addressed using the Modeled Emission Rates for Percursors (MERPs)

approach as discussed in Section 5.8 below. In addition, hexane and ammonia, toxic

air pollutants to be emitted in quantities of one ton per year or greater, were evaluated

using Ohio EPA’s air toxics modeling procedures.

5.2 Significant Impact Analysis

The criteria pollutant air quality analysis was conducted in two phases: an initial or

significant impact analysis, and a refined phase including an increment analysis and a

NAAQS analysis. In the significant impact analysis, the calculated maximum impacts

were determined for each pollutant with an emissions increase that exceeds the PSD

significant emission level. These impacts determine the net change in air quality

resulting from the proposed modification. Five years of meteorological data were used

in the significant impact analysis. Maximum modeled concentrations were compared to

the pollutant-specific significance levels for all pollutants and averaging times except for

the 1-hr NO2 and 24-hr PM2.5 impacts. For these pollutants and averaging periods, the

five year average of the maximum impact at each receptor will be used to assess

significance. The PSD Class II Significant Impact Levels listed in Table 4 are

appropriate for this site, which is greater than 300 km from any Class I area. See Ohio

Engineering Guide 69 at p.21.

Pollutants with impacts that exceed the ambient air significance levels, as defined in 40

CFR 51.165, were included in both the NAAQS and increment analyses. In these latter

analyses, impacts from the HBI Facility were added to concentrations calculated from

other nearby sources, plus a regional background concentration (for the NAAQS

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analysis only). The resultant total concentrations were compared to the NAAQS and

increments to determine compliance.

Table 4. PSD Class II Significant Impact Levels

Pollutant Averaging TimePSD Class II Significant Impact Levels (µg/m3)a

PM10 24-hour 5.0Annual 1.0

PM2.5a 24-hour 1.2Annual 0.3

NO2 1-hour 7.5b

Annual 1.0CO 1-hour 2000

8-hour 500aPlease note that on January 22, 2013, the US Court of Appeals for the District of Columbia Circuit Court granted a request from the EPA to vacate and remand the PM2.5 SILs. USEPA draft modeling guidance (August 1, 2016, Revised August 18, 2016), issued subsequent to the remand, continues to allow for use of the SILs listed above to justify PSD permitting decisions for PM2.5 NAAQS and increment evaluations. bPlease note that there is no 1-hr NO2 SIL promulgated at 40 CFR 51.165. Consistent with to the June 28, 2010 EPA Policy Memorandum from Anna Marie Wood to the Regional Air Directors, an interim 1-hr NO2 SIL of 4 ppb (7.5µg/m3) has been adopted by the OEPA. 5.3 Preconstruction Monitoring

The concentrations calculated in the significant impact analysis were also compared to

the PSD pre-construction monitoring exemption levels shown below in Table 5. If these

exemption levels are not exceeded, OEPA has the discretion to exempt from the

requirement to collect pre-construction ambient monitoring data. The representative

background pollutant concentrations were incorporated in the analysis. As will be

shown, the ambient monitoring exemption level is calculated to be exceeded for PM10

and CO. We therefore request that the existing representative monitoring data be

allowed for use in lieu of site-specific pre-construction monitoring data to avoid

unreasonable delay.

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Table 5. PSD Preconstruction Monitoring Exemption Levels

Pollutant Averaging TimeMonitoring Exemption

Levels (µg/m3) CO 8-hour average 575NO2 Annual average 14PM10 24-hour average 10

5.4 NAAQS Analysis

Following the determination of significant impacts, a refined air quality analysis to

determine compliance with the NAAQS was conducted. This analysis was conducted to

determine compliance with the NAAQS only for pollutants modeled as having significant

impacts in the initial analysis. The receptors modeled in the NAAQS analyses were

limited to those showing a significant impact for each pollutant. Each source's potential

emission rate was used. Five years of meteorological data were again used in this

analysis.

Nearby Source Inventory

Off-site sources were included in the NAAQS and increment analyses. A 50km radius

was initially used to define the screening area. A list of sources that are located within

the screening area was obtained from the OEPA and Michigan Department of

Environmental Quality (MDEQ). Section 8.3.3.b of Appendix W to 40 CFR Part 51

states that the number of nearby sources to be explicitly modeled is expected to be few,

except in unusual situations. There are over 1,200 individual emission sources located

within 50km of the IU site. Appendix W states that the sources to be included will

usually be located within the first 10 to 20km from the source under consideration. In

addition, it states that identification of nearby sources calls for the exercise of

professional judgment by the appropriate reviewing authority. Further, EPA’s Guidance

for PM2.5 Permit Modeling reiterates the Appendix W emphasis on a 10km screening

radius for determining which nearby sources to include in the cumulative modeling

analysis.

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Modeling was conducted for the nearby sources located in excess of 20km from the

proposed site to determine their potential impact. This modeling demonstrates that the

annual PM2.5 contribution from these distant “nearby” sources is approximately 0.75

µg/m3. The annual background PM2.5 concentration of 8.64 µg/m3 is over 10 times

greater than the contribution of these distant sources. These distant sources are more

than adequately represented in the PM2.5 annual background concentration. In the

PM2.5 annual NAAQS analysis, IU therefore only included those nearby PM2.5 sources

located within the first 20km of the proposed site.

The OEPA does not maintain a database of emission rates based on the maximum

allowable emission limits that are needed for a NAAQS modeling demonstration. These

values will be obtained by reviewing permit files.

Once all sources in the screening area were identified, we employed the NC Division of

Air Quality's (DAQ) 20D screening criterion to eliminate sources outside of the

significant impact area, but within the screening area, that were not likely to influence

the analysis. Total facility potential emissions (i.e., all sources at a facility) were used in

the 20D evaluation. All major sources located within the significant impact area were

included (i.e., no sources were screened out).

Since OEPA does not maintain a database of potential source emissions, the upper

bound of the source classification was used in the 20D screening. For example, if a

source's potential to emit PM10 was not known, but it was known that the source is

minor source for Title V permitting purposes, the source was conservatively assumed to

have the potential to emit at the Title V permitting threshold of 100 tons per year PM10.

This minimized the need to conduct a detailed file review for sources that could be

screened from evaluation based upon source classification. The results of the source

screening are provided in Attachment A.

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NAAQS Compliance Assessment Ambient background concentrations (as discussed in more detail in Section 4.3) were

added to the modeled concentrations to assess NAAQS compliance. The modeled and

monitored values shown in Table 6 were used for this assessment. The NAAQS are

shown in Table 7.

Table 6. Monitored and Modeled Values Used to Assess NAAQS Compliance

Pollutant Averaging Time Monitored Value Modeled ValueCO 1-hour & 8-hour Maximum over

three yearsHighest, second high over 5 years

NO2 Annual Maximum over three years

Maximum over 5 years

1-hour 3 year average of 98% daily max

5 year average of 98% daily max

PM10 24-hour Maximum value over 3 years

Highest, sixth high over 5 years

PM2.5 Annual 3 year average 5 year average24-hour 3 year average of

98% daily max5 year average of

98% daily max

Table 7. National Ambient Air Quality Standards

Pollutant Averaging Time

National Ambient Air Quality Standards (µg/m3)

Primary Secondary PM10 24-hour 150 150 NO2 1-hour 188 --

Annual 100 100 CO 1-hour 40,000 --

8-hour 10,000 --

5.5 PSD Increment Analysis

The increment consumption analysis included emissions from all proposed increment

consuming sources. Compliance with the PSD increments was based on cumulative

impacts of the HBI Facility and other viable increment consuming sources identified in

the nearby source emissions inventory. Potential emissions were conservatively used

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as an alternate to actual emissions in assessing compliance. The resultant

cummulative impacts were compared to the PSD Class II increment levels. The highest

modeled annual averages were used for evaluating compliance with the annual

increments and the high-second-high values were used for the evaluation of compliance

with the short-term increments. The PSD Class II increments are shown in Table 8.

The OEPA also generally requires a demonstration that the Project’s emissions will not

exceed 50%of the federal increments. However, for sources locating on qualifying

brownfield sites, Ohio EPA policy allows the source to consume up to 83% of the

increment. The Project is located at the Ironville brownfield site, which has been

recognized by Ohio EPA as a qualifying brownfield that has been prepared for

productive re-use under the Ohio Voluntary Action Program.

Table 8. PSD Increments

Pollutant Averaging TimePSD Increments (µg/m3) Class II Class I

PM10 24-hour 30 8 Annual 17 4

NO2 Annual 25 2.5

Since there is no federal 1-hr NO2 increment, we have also demonstrated that the

Project impacts, using the maximum modeled concentrations, do not exceed the 1-hr

NO2 NAAQS. 5.6 NO2 Analyses

Following USEPA guidance, the NO2 modeling analyses used the recommended three

tier screening approach. Initially, Tier 1 was employed with the conservative assumption

that 100% of the available NOx converts to NO2. Since NO2 impacts exceed the SILs,

the Tier 2 (Ambient Ratio Method, ARM2) was employed for the 1-hr conversion with

the EPA default minimum and maximum ambient ratios of 0.5 and 0.9, respectively.

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Tier 3 was employed in the cumulative NO2 NAAQS evaluation. Tier 3 accounts for the

chemical reactions that convert NOx to NO2 in the presence of ozone.

Tier 3 Option There are two Tier 3 methods currently available in AERMOD for simulating this

conversion: the Ozone Limiting Method (OLM) and the Plume Volume Molar Ratio

Method (PVMRM). Both methods are currently implemented through a regulatory

default option in AERMOD. We employed PVMRM. An in-stack ratio of 0.50 was

assumed for all HBI sources. Consistent with EPA guidance, an in stack ratio of 0.20

was used for all off-site sources as each is located greater than 1km away from the HBI

Facility.10 In addition, the default NO2/NOx equilibrium ratio of 0.90 was employed.

Hourly ozone concentrations from the Allen Park monitor in Michigan (AQS #26-163-

0001), concurrent with the 2013-2017 meteorological data period, were used. Any

missing data from this monitor were substituted with values from the Erie monitor in

Toledo (AQS #39-095-0024). The Erie monitor values was not used as the primary

monitor because it is only active during the O3 season (April through October). 5.7 Intermittent Emissions

Emissions from sources that emit intermittently (i.e., emergency generators and the

flare) were not included in determination of compliance with the short-term standards

(i.e., 1 hour through 24 hour) as they operate for short durations and infrequently.

Moreover, these intermittent sources replace sources that do not operate at normal

rates during malfunctions or during emergencies. Such events are not considered to be

normal operations and are not included in establishing emission limits per the Guideline

at 8.2.2. The generator and firewater pump will only be operated for testing which will

last for less than a few hours and for less than 500 hours per year each. The startup

and shutdown events associated with flaring will last for less than four hours per event

with 24 or fewer events per year.

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5.8 Secondary PM2.5 Analyses

In May of 2014, the EPA issued its final guidance for assessing primary and secondary

formation of fine particulate matter (PM2.5) in NAAQS and increment compliance

demonstrations under PSD.11 On June 5, 2018, at the USEPA Regional, State, and

Local Modeler’s Workshop, the USEPA announced proposed revisions to the 2014

Guidance. While the announced revisions are not official EPA guidance, the USEPA

outlines two cases for assessing the primary and secondary PM2.5 impacts. The

appropriate case to use depends on the magnitude of direct PM2.5 and precursor NO2

and SO2 emissions. Case 1 is applicable if the emissions increase of both direct PM2.5

and secondary NOx and SO2 emissions are below the SER. Case 2 is applicable if the

direct PM2.5 emissions increase or the NOx and/or SO2 emissions increase is greater

than the respective SER. Case 2 is applicable to the project as the direct PM2.5

emissions are projected to exceed 10 tons per year and NOX emissions are projected

to exceed 40 tons per year. In this case, a PM2.5 compliance demonstration is required

for the direct PM2.5 emissions based on approved dispersion modeling techniques. T

he potential impact of the precursor emissions must also be evaluated. The potential

precursor emissions impact on secondary PM2.5 formation may be completely

qualitative in nature, may be based on a hybrid of qualitative and quantitative

assessments utilizing existing technical work, or may be a full quantitative

photochemical grid modeling exercise. According to the PM2.5 guidance (page 24),

"the EPA anticipates only a few situations would require explicit photochemical grid

modeling."

We have modeled the direct PM2.5 emissions using approved dispersion techniques

and have used the latest Modeled Emissions Rates for Precursors (MERPs) approach

to assess the impacts of precursor emission on secondary PM2.5 formation.12

The potential precursor emissions impact on secondary PM2.5 formation for the

NAAQS and increment analyses was based on the Modeled Emission Rate for

Precursor (MERP) approach. Equation Number 2 from the MERP guidance was used to

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derive the secondary impact of the project. Hypothetical Source No. 11 in Macomb

County Michigan was used with 500TPY emission rate and 90m release.

The secondary air quality impact from the IU project was then calculated as follows per

Equation No. 2 of the MERPs guidance:

IU Impact = IU emission rate x (Modeled air quality impact from the hypothetical source ÷ Modeled emission rate from the hypothetical source)

Total NAAQS impact = IU Impact + Modeled Direct PM2.5 Impact + Background Concentration Total increment impact = IU Impact + Modeled Direct PM2.5 Impact

5.9 Ozone Analyses

There are currently no regulatory photochemical models available to evaluate smaller

spatial scales or single-source impacts on ozone concentrations. Since ozone is

formed from precursor pollutants, assessment of ambient ozone impacts is typically

conducted on a regional basis using resource-intensive models such as the EPA

Community Multiscale Air Quality (CMAQ) model. However, sources subject to PSD

review are required to conduct a source impact analysis and demonstrate that a

proposed source will not cause or contribute to a violation of any NAAQS or applicable

increment. Qualitative ozone analyses have typically been performed in recent PSD

applications to evaluate whether ozone precursor emissions (NOx and VOC) will

significantly impact regional ozone formation.

Potential emissions of NO2 from the proposed HBI Facility will be above the 40 ton per

year major source threshold; however, VOC emissions will be below 100 tons per year.

The EPA and permitting authorities have historically used the 100 ton per year threshold

to assess whether a detailed air quality analysis should be conducted for ozone.13

According to EPA, although this threshold has not been revisited since promulgation of

the 8-hour ozone NAAQS, it is unlikely that a source emitting below this level would

contribute to a violation of the 8-hour ozone NAAQS.

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However, we have used the MERPs approach to assess the impacts of precursor

emission on O3. Hypothetical Source No. 11 in Macomb County Michigan was again

used with 500TPY emission rate and 90m release. The IU project impacts were then

calculated as follows:

IU NOx Contribution to Ozone = IU NOx annual emission rate ÷ NOx MERP

IU VOC Contribution to Ozone = IU VOC annual emission rate ÷ VOC MERP

IU Total Ozone Potential Impact (as a percentage of the 1.0 ppb ozone SIL) = IU

NOx contribution + IU VOC contribution

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6.0 MODEL RESULTS 6.1 Significant Impact Analysis Results The Project will result in significant impacts for NO2 (1-hr), PM10, and PM2.5.

Insignificant impacts are calculated for annual NO2 and CO. The Class II significant

impact analysis results are presented in Table 9. A cumulative analysis was therefore

conducted for the 1-hour NO2, PM10, and PM2.5 NAAQS. A cumulative analysis was

also conducted for the PM10 and PM2.5 increments. Table 9 also shows that the

significant monitoring concentrations (SMC) for PM10 and PM2.5 will be exceeded. We

request that the existing representative monitoring data be used in lieu of site-specific

pre-construction monitoring data. NO2 and CO concentrations will not exceed the

SMCs.

Table 9. Class II Significant Impact Analysis Results

Pollutant Averaging

Period

Maximum Modeled Impact (μg/m3)

PSD Significant

Class II Impact Level

(μg/m3)

Significant Monitoring

Concentration (μg/m3)

Maximum Distance to a Significant Impact (km)

NO2a 1-hr 14.5 7.5 -- 1.6

Annual 1.25 1.0 14 0.59

CO 1-hr 3,010 2000 -- 0.82

8-hr 1,744 500 575 2.5

PM10 24-hr 27.2 5.0 10 2.2

Annual 2.53 1.0 -- 0.9

PM2.5b 24-hr 7.03 1.2 0 2.9

Annual 0.97 0.3 -- 1.6 aNO2 impacts include ARM of 0.75 for the annual average and ARM2 for the 1-hr average. bPM2.5 impacts include contribution of secondarily formed PM2.5 of 0.07 and 0.002 µg/m3 for the 24-hr and annual averages, respectively.

N/A – Not applicable, impacts calculated to be insignificant. 6.2 1-hr NO2 Increment and Air Toxics Analysis Results The results of the state 1-hr NO2 increment and air toxics modeling for hexane are

shown in Table 10. As shown, modeled impacts are acceptable.

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Table 10. State 1-hr NO2 Increment and Air Toxics Analysis Resultsa

Pollutant Averaging

Period

Maximum Modeled Impact (μg/m3)

Standard (μg/m3)

NO2 1-hr 38.9 188

Hexane 1-hr 0.08 4,196

Ammonia 1-hr 261 415 aProject only emissions modeled. 100% NOx to NO2 conversion assumed.

6.3 NAAQS Analysis Results Following the determination of significant impacts, an analysis was conducted to assess

compliance with the NO2, CO, PM10 and PM2.5 NAAQS. All major and minor sources

located within 50km of the proposed facility were evaluated for inclusion in the NO2,

CO, PM10 and 24-hr PM2.5 model in assessing compliance. For the reasons

discussed in Section 5.4, only sources within 20km of the proposed site were

considered for inclusion in the annual PM2.5 NAAQS analysis. Sources located beyond

20km were addressed in the background concentrations added to the model results to

assess compliance.

The results of the NAAQS analysis are presented in Table 11. The secondary PM2.5

impacts presented in Section 6.5 below were added to the total modeled impacts in

assessing compliance. As shown, the model demonstrates compliance. 6.4 Increment Analysis Results Evaluation of compliance with the short-term increments was based upon the highest-

second-high value from the five years of meteorology. The maximum annual

concentrations were used to assess compliance with the annual increments. The

results of the increment analysis are presented in Table 12. As shown, the cumulative

model demonstrates compliance with all PSD increments. The model indicates that the

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Table 11. NAAQS Analysis Results

Pollutant Averaging

Period

Modeled Concentration

(µg/m3)

Background Concentration

(µg/m3)

Total Concentration

(µg/m3)Standard (µg/m3) Comment

NO2 1-hour 168.5a

Season by hour values added within model

168.5 188 Compliant.

Annual 7.52 17.7 25.2 100 Compliant.

PM2.5 24-hour 9.38b 21.5 30.9c 35 Compliant. Total includes secondary PM2.5

contribution of 0.07 µg/m3

Annual 2.08 8.22 10.3c 12 Compliant. Total includes secondary PM2.5 contribution of 0.002 µg/m3.

CO 1-hour 2,845 2,743 5,588 40,000 Compliant8-hour 1,429 1,863 3,292 10,000 Compliant

PM10 24-hour 45.2 35.0 80.2 150 CompliantaBased on the 98th percentile of the annual distribution of maximum daily 1-hour concentrations, averaged across the 5 years of meteorological data modeled. PVMRM was employed for the 1-hr calculations.

bBased on the 98th percentile of the annual distribution of maximum daily concentrations, averaged across the 5 years of meteorological data modeled. cIncludes contribution of secondarily formed PM2.5 of 0.07 and 0.002 µg/m3 for the 24-hr and annual averages, respectively.

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Project impacts will exceed the OEPA guideline of 50% of the increment for the 24-hr

averages. As shown in Figures 11 and 12, the PM10 and PM2.5 24 hour 50%

increment exceedences are limited to the immediate vicinity of the Project’s fenceline

(the exceedence locations are indicated with the blue numbers). In addition, there are

no impacts that exceed 83% of the increments, which is the applicable increment

consumption threshold for this Project allowed for the redevelopment of brownfields.

6.5 Secondary PM2.5 Analysis Results

Table 13 presents the MERPs hypothetical source data, including emissions and

impacts, as well as the calculated secondary impacts from the proposed HBI project.

The secondary PM2.5 impacts (sulfate and nitrate) were added to the modeled direct

impacts and compared to the Class II NAAQS and increments.

6.6 Ozone Analysis Results

Table 13 presents the MERPs hypothetical source data, including emissions and

impacts, as well as the ozone impact analysis results. As shown, the HBI project will

not result in ozone impacts in excess of the ozone SIL. 6.7 Model Input and Output Files

The modeling input and output files are provided on the attached CD. Model summary

results are presented in Attachment B to this report. The summary results list the model

file names associated with each phase of the analysis.b

b As a general rule, the AERMOD input files have a “dta” extension. The AERMOD output files have a “lst” extension.

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Table 12. PSD Increment Analysis Results

Pollutant Averaging

Period Source Group

Modeled Concentration

(µg/m3)a,bStandard (µg/m3) Comment

PM2.5 24-hour

PM25INC 7.16 9.0 Cumulative impacts, HBI and other inc. consumers

CLIFFS 7.02 4.5 50% increment comparison. HBI impacts only.7.02 7.5 83% increment comparison. HBI impacts only.

Annual PM25INC 1.18 4.0 Cumulative impacts, HBI and other inc. consumersCLIFFS 1.07 2.0 50% increment comparison. HBI impacts only.

PM10

24-hour

PMNOXINC 26.3 30.0 Cumulative impacts, HBI and other inc. consumers

CLIFFS 23.5 15.0 50% increment comparison. HBI impacts only.23.5 24.9 83% increment comparison. HBI impacts only.

Annual PMNOXINC 4.20 17.0 Cumulative impacts, HBI and other inc. consumers

CLIFFS 2.51 8.5 50% increment comparison. HBI impacts only.

NOx Annual PMNOXINC 7.52 25.0 Cumulative impacts, HBI and other inc. consumers

CLIFFS 1.25 12.5 50% increment comparison. HBI impacts only aBased on the maximum highest second high value from the five years of meteorology. bModeled PM2.5 impacts include a secondary PM2.5 contribution of 0.07 and 0.002 µg/m3 for the 24-hr and annual averages, respectively.

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Figure 11. PM2.5 24-Hour 50% Increment Exceedence Locations

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Figure 12. PM10 24-Hour 50% Increment Exceedence Locations

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Table 13. Hypothetical Source Data and Calculated HBI Secondary PM2.5 Impacts

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Table 14. Hypothetical Source Data and Calculated Ozone Impacts (as a percentage of the Air Quality Index)

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7.0 CLASS II VISIBILITY ANALYSIS The CAA Amendments of 1977 require evaluation of new and modified emission

sources to determine potential impacts on visibility. The maximum increase in hourly

particulate matter and NOX emissions from the proposed HBI Facility were used as

input parameters in the visibility analysis. Emissions were evaluated as described in the

EPA Workbook for Plume Visual Impact Screening and Analysis14 to determine potential

contribution to atmospheric discoloration and visual range reduction.

Generally, atmospheric discoloration occurs when NO emissions from combustion

sources react in the presence of atmospheric oxygen to form NO2, a reddish-brown gas.

Another form of atmospheric discoloration may be caused by particulate emissions and

secondary aerosols formed by gaseous precursor emissions. The visual range

reduction (increased haze) is caused primarily by particulate emissions and secondary

aerosols such as sulfates and nitrates. Both secondary sulfate and primary particulate

emissions are accounted for in the analysis. Emission of other pollutants do not

materially affect visibility.

U.S. EPA visibility impairment analysis guidelines were followed in conducting the

analysis. The analysis was performed for the Cuyahoga Valley National Park, located

approximately 155km east-southeast of the proposed HBI site. The Park is not a Class

I area.

This analysis requires inputs of emission rates (PM and NOX), regional visual range,

distance between the source and the object of study, and worst-case dispersion

parameters (i.e., wind speed and stability). Outputs from the model include:

• Plume contrast against the sky and terrain; and,

• Perceptibility of the plume (Delta E criteria).

Emission rates for PM and NOx for the analyses were set to 33 and 109 lb/hr,

respectively. These emissions represent the total facility, short-term proposed

emissions. The background visual range was set to 25km, which was determined from

Figure 9 of the VISCREEN manual. The VISCREEN default screening values for Delta

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E (2.0) and contrast (0.05) were assumed.

As shown in Table 14, there are no exceedances of the visibility screening criteria. The

Project should therefore not affect visibility at the Cuyahoga Valley National Park. The

VISCREEN model files are provided on the enclosed CD.

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Table 15. Level-1 Class II Visibility Analysis Results for Cuyahoga Valley National Park

Viewing Background

Theta (degrees)

Azimuth (degrees)

Distance (km)

Alpha (degrees)

Delta E Green ContrastCriterion Plume Criterion Plume

SKY 10 84 155 84 2.0 0.003 0.05 0.000SKY 140 84 155 84 2.0 0.001 0.05 0.000TERRAIN 10 84 155 84 2.0 0.000 0.05 0.000TERRAIN 140 84 155 84 2.0 0.000 0.05 0.000

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8.0 CLASS I AREA IMPACTS 8.1 Class I AQRV Analysis There are no Class I areas located within 300km of the HBI Facility (please see Figure

13).c The closest Class I area is the Otter Creek Wilderness Area, located 436km to the

southeast. The Federal Land Manager’s (FLM) Q/D (maximum daily emissions in tons

per year over distance in kilometers) method was used to determine the potential for

adverse Class I impacts for each Class I area. The Q/D value calculated based upon a

total PM10, NOx, SO2 (H2SO4 emissions are negligible) emission rate of 640 tons per

year and a distance of 436km is calculated to be 1.5. As this is below 10, per the the

FLM's Air Quality Related Values Work Group (FLAG) document.15, no Air Quality

Related Values (AQRV) evaluation is required. A notification was sent to the FLM on

August 7, 2017. The FLM responded on August 14, 2017 and confirmed that an AQRV

analysis would not be required for the proposed project.

8.2 Class I Increment Analysis Since the closest Class I area is over 300km away and the the Q/D is less than 10,

OEPA does not require any Class I modeling to assess Class I increments (see Answer

21 in Engineering Guide 69). Therefore, no Class I increment analysis was conducted.

c Class I areas are pristine areas (e.g., National Parks and Wilderness Areas) that have been designated by Congress and are afforded a greater degree of air quality protection. All other areas are designated as Class II areas.

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Figure 13. Class I Areas Located within Three Hundred Kilometers

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Iron Units LLC

REFERENCES

1. Ohio EPA. 1986. Air Toxics Policy. Option A, Review of New Sources of Air Toxics Emissions. 2. Engineering Guide #69, Air Dispersion Modeling Guidance, Ohio EPA, Division of Air Pollution Control, July 22, 2014 (Revised). 3. Guidelines on Air Quality Models, (Revised). Appendix W of 40 CFR Part 51, 82 FR 5182, January 17, 2017. 4. Auer, Jr., A.H. "Correlation of Land Use and Cover with Meteorological Anomalies." Journal of Applied Meteorology, 17:636-643, 1978. 5. Haul Road Workgroup Final Report, EPA Region 5, December 6, 2011. 6. Guideline for Determination of Good Engineering Practice Stack Height (Technical Support Document for Stack Height Regulations (Revised). EPA-450/4-80-023R, U.S. Environmental Protection Agency, June 1985. 7. Sierra Club v. EPA, No. 10-1413, 2013 WL 216018 (Jan. 22, 2013). 8. Ambient Monitoring Guidelines for Prevention of Significant Deterioration, EPA-450/4-87-007, USEPA, May 1987. 9. Ambient Monitor Guidelines for Prevention of Significant Deterioration, EPA-450/4-87-007, USEPA, May 1987. 10 . U.S. EPA, Clarification on the Use of AERMOD Dispersion Model for Demonstrating Compliance with the NO2 National Ambient Air Quality Standard, September 30, 2014. 11. U.S. EPA, Guidance for PM2.5 Permit Modeling, EPA-454/B-14-001, May 2014. 12. U.S. EPA, Guidance on the Development of Modeled Emission Rates for Precursors (MERPs) as a Tier 1 Demonstration Tool for Ozone and PM2.5 under the PSD Permitting Program, April 30, 2019. 13. See footnote 1 to 40 CFR 51.166(i)(5)(i)(f) and USEPA’s 1990 NSR Workshop Manual, page C.28., footnote b. 14. Workbook for Plume Visual Impact Screening and Analysis. US EPA, EPA Pub. No. 450/4-88-015. RTP, NC. September 1988. 15. Federal Land Managers Air Quality Related Values Workgroup (FLAG) – Phase I Report-Revised (2010), US Forest Service, National Parks Service, US Fish and Wildlife Service, 2010.

Page 280: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

IronUnits LLC

ATTACHMENT A MODELED SOURCE INPUT DATA

VOLUME SOURCE SIGMA CALCULATIONS

LAND USE ANALYSIS OFF-SITE SOURCE SCREENING

FLM CORRESPONDENCE

Page 281: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Point Source Model Input (NAD83, Zone 17)(Last Update 9-13-19)

Source ID Source Description Easting (m) Northing (m)

Base Elevation

(ft)

Stack Height

(ft) Temp (F)

Exit Velocity (ft/sec)

Stack Diameter

(ft) PM25PM-25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO Hexane NH3MTR_5 Hopper to Conveyor Transfer Tower (Baghouse) 293292.61 4616948.13 589.99 29.0 -460.0 16.22 2.0 0.065 0.009 0.065 0.009 0.000 0.000 0.000 0.000 0.000TR_1 Transfer Tower-I (Baghouse) 293633.73 4616748.43 590.03 61.0 -460.0 72.97 1.3 0.131 0.018 0.131 0.018 0.000 0.000 0.000 0.000 0.000TR_6 Transfer Tower-II (Baghouse) 293329.26 4616357.30 595.18 39.0 -460.0 63.53 1.2 0.087 0.050 0.087 0.050 0.000 0.000 0.000 0.000 0.000TR_7 Transfer Tower-III (Baghouse) 293405.16 4616303.16 594.39 75.0 -460.0 63.53 1.2 0.087 0.050 0.087 0.050 0.000 0.000 0.000 0.000 0.000TR_10 Oxide Day Bin Drops with 2 Baghouses 293463.88 4616386.03 593.50 105.0 -460.0 70.53 2.5 0.445 0.359 0.445 0.359 0.000 0.000 0.000 0.000 0.000SR_1 Screen Building Baghouse Exhaust 293526.08 4616472.96 589.01 90.0 -460.0 70.48 2.0 0.285 0.250 0.285 0.250 0.000 0.000 0.000 0.000 0.000TR_13a Conveyor to Bucket Elevator with Baghouse 293703.13 4616347.72 587.63 185.0 -460.0 75.19 1.0 0.076 0.067 0.076 0.067 0.000 0.000 0.000 0.000 0.000TR_13b Conveyors with Fines Transfer Tower 293597.34 4616434.30 587.24 75.0 -460.0 75.19 1.0 0.076 0.081 0.076 0.081 0.000 0.000 0.000 0.000 0.000TR_14 Coating Stroage and Mixing and Fines Transfer (BH) 293544.89 4616470.27 589.96 62.0 -460.0 19.18 1.0 0.019 0.019 0.019 0.019 0.000 0.000 0.000 0.000 0.000TR_17 Transfer Tower 1 Scrubber 293759.97 4616322.29 587.43 60.0 -460.0 83.16 1.2 0.114 0.076 0.114 0.076 0.000 0.000 0.000 0.000 0.000TR_18 Transfer Towers 2 & 3 Scrubber 293651.70 4616184.56 591.54 60.0 -460.0 63.67 1.3 0.114 0.076 0.114 0.076 0.000 0.000 0.000 0.000 0.000TR_23 HBI Transfer Tower to Loadout Scrubber 293729.34 4616181.50 589.50 55.0 -460.0 69.66 1.0 0.070 0.041 0.070 0.041 0.000 0.000 0.000 0.000 0.000TR_24 HBI Transfer to Loadout Silo to Loadout Scrubber 293603.85 4616139.17 592.06 125.0 -460.0 69.66 1.0 0.070 0.035 0.070 0.035 0.000 0.000 0.000 0.000 0.000TR_25 HBI Truck Loadout Scrubber 293592.40 4616146.45 591.99 125.0 -460.0 76.74 1.2 0.105 0.105 0.105 0.105 0.000 0.000 0.000 0.000 0.000TR_28a Oxide Conveyor to Furnace Feed Conveyor with BH 293723.29 4616395.68 589.44 87.9 -460.0 61.95 1.0 0.063 0.055 0.063 0.055 0.000 0.000 0.000 0.000 0.000TR_28b Charge Hopper Scrubber 293745.59 4616412.54 589.60 435.4 86.0 47.65 0.9 0.101 0.101 0.101 0.101 2.021 2.021 2.822 0.000 0.000P_1 Bottom Seal Gas Scrubber 293757.01 4616413.58 589.27 438.0 132.8 91.67 3.2 2.612 2.612 2.612 2.612 0.429 0.429 986.027 0.000 0.000P_2 Reformer Flue Gas Exhaust 293604.09 4616495.51 587.83 196.9 595.4 66.03 14.0 18.712 18.712 18.712 18.712 99.747 99.747 52.350 0.595 0.000P_3 Hot Briquette Dust Collection 293758.64 4616412.49 589.24 438.0 86.0 91.07 3.9 4.100 4.100 4.100 4.100 3.939 3.939 912.014 0.000 0.000P_4 Briquette Cooling System Vent 293746.49 4616393.91 589.40 451.1 149.0 57.01 4.7 3.303 3.303 3.303 3.303 0.000 0.000 594.075 0.000 0.000P_5 Degasser Exhaust 293635.63 4616540.04 588.22 75.5 122.0 61.98 2.4 0.000 0.000 0.000 0.000 0.000 0.000 110.057 0.000 3.970P_6a Flare - Startup & Shut Down 293584.32 4616473.94 588.39 141.8 1832.0 65.60 7.2 0.000 0.146 0.000 0.146 1.331 0.000 0.000 0.000 0.000P_6b Flare - Pilot 293584.32 4616473.94 588.39 109.3 140.0 0.15 4.2 0.005 0.005 0.005 0.005 0.049 0.049 0.224 0.000 0.000P_7 Cooling Tower 293650.31 4616607.37 588.39 57.1 70.0 0.03 25.0 0.013 0.013 0.021 0.021 0.000 0.000 0.000 0.000 2.250P_8 Emergency Fire Water Booster 293798.94 4616419.94 589.24 9.8 877.0 920.84 0.4 0.000 0.007 0.000 0.007 0.117 0.000 0.000 0.000 0.000P_9 Emergency Generator 293769.49 4616529.17 588.94 25.0 877.0 510.23 0.8 0.000 0.058 0.000 0.058 1.611 0.000 0.000 0.000 0.000P_10 Admin Building Generator 293861.87 4616470.59 588.62 7.5 1074.0 139.33 0.3 0.000 0.004 0.000 0.004 0.050 0.000 0.000 0.000 0.000

Potential Emissions (lb/hr)

Page 282: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Volume Source Inputs

Source ID Source Description Easting (m) Northing (m)

Base Elevation

(ft)

Release Height

(ft)Sigma Y

(ft)Sigma Z

(ft) PM25PM-25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO Hexane NH3MTR_1 Boat Unloading 293182.49 4617050.42 579.86 23.0 5.8 5.3 0.00E+00 5.78E-03 0.00E+00 3.82E-02 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00MTR_2 Hopper to Conveyor Drop 293186.90 4617047.15 580.25 9.8 5.8 2.3 0.00E+00 5.78E-03 0.00E+00 3.82E-02 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00MTR_3 Conveyor to Stacker Drop 293260.40 4616975.59 586.88 16.4 5.8 3.8 0.00E+00 5.78E-03 0.00E+00 3.82E-02 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00MTR_4 Stacker to Hopper 293292.61 4616948.13 589.99 29.3 5.8 6.8 0.00E+00 1.89E-03 0.00E+00 1.24E-02 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_2 Conveyor to Stacker Machine 293472.49 4616539.34 589.57 55.1 5.8 12.8 6.08E-02 6.28E-03 4.01E-01 4.15E-02 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00WE_1 Oxide Stockpile Wind Erosion 293437.12 4616543.52 588.55 52.5 100.7 12.2 1.76E-02 8.79E-03 4.39E-02 2.20E-02 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_3 Stacker to Stockpile 293509.16 4616512.05 590.58 52.5 5.8 12.2 5.60E-02 5.78E-03 3.70E-01 3.82E-02 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_4 Oxide Reclaim using Bucket Wheel to Conveyor 293504.74 4616506.11 590.26 52.5 5.8 12.2 2.06E-02 5.78E-03 1.36E-01 3.82E-02 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_5 Conveyor from Reclaim Machine to Main Conveyor 293468.07 4616533.40 588.88 13.6 5.8 3.2 2.24E-02 6.28E-03 1.48E-01 4.15E-02 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_8 Oxide Lumps Conveyor Transfer to Stockpile 293531.05 4616486.84 589.34 62.7 18.7 29.1 3.42E-04 5.78E-06 2.26E-03 3.82E-05 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00WE_2 Oxide Lumps Stockpile Wind Erosion 293531.05 4616486.84 589.34 62.7 18.7 29.1 3.59E-05 1.80E-05 8.98E-05 4.49E-05 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00FEL_1 FEL for Lump Reclaim Fugitive on Unpaved 293531.05 4616486.84 589.34 62.7 18.7 29.1 3.68E-04 3.72E-06 3.68E-03 3.72E-05 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_9 Oxide Lumps Drop from FEL to Truck 293531.05 4616486.84 589.34 62.7 18.7 29.1 7.89E-03 1.16E-04 5.21E-02 7.64E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_11 Oxide Fines to Stockpile 293575.15 4616395.92 588.88 21.3 5.8 5.0 1.33E-03 7.10E-04 8.81E-03 4.69E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00WE_3 Oxide Fines Stockpile Wind Erosion 293575.15 4616395.92 588.88 21.3 5.8 5.0 2.77E-04 1.39E-04 6.93E-04 3.46E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00FEL_2 FEL for Oxides Fine Reclaim Fugitives on Unpaved 293575.15 4616395.92 588.88 21.3 5.8 5.0 3.68E-04 2.07E-04 3.68E-03 2.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_12 Oxide Fines from FEL to Truck 293575.15 4616395.92 588.88 9.8 5.8 2.3 1.61E-02 1.42E-02 1.07E-01 9.37E-02 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_15 REMET Drop to Stockpile 293705.30 4616289.35 588.22 10.5 5.8 2.4 9.68E-03 7.10E-03 6.40E-02 4.69E-02 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00WE_4 REMET Stockpile Wind Erosion 293705.30 4616289.35 588.22 10.5 5.8 2.4 1.51E-02 7.55E-03 3.77E-02 1.89E-02 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_16 REMET Transfer from FEL to Hopper 293447.27 4616374.58 595.37 62.7 18.7 29.1 1.69E-02 7.10E-03 1.12E-01 4.69E-02 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_19 HBI Transfer from Conveyor to Stacker 293772.82 4616317.35 586.88 42.1 5.8 9.8 1.56E-02 8.66E-03 3.57E-02 1.98E-02 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_20 HBI Transfer from Stacker to Stockpile 293787.09 4616306.73 587.34 19.7 5.8 4.6 2.53E-02 1.41E-02 5.79E-02 3.21E-02 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00WE_5 HBI Stockpile Wind Erosion 293787.09 4616306.73 587.34 19.7 64.9 4.6 1.82E-03 9.10E-04 4.55E-03 2.28E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00FEL_4 HBI Reclaim FEL fugitives 293744.50 4616227.82 588.12 3.3 5.8 0.8 7.25E-03 5.45E-04 7.25E-02 5.45E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_21a HBI Reclaim Bucket Wheel to Conveyor 293787.09 4616306.73 587.34 19.7 5.8 4.6 2.25E-02 7.97E-03 5.15E-02 1.82E-02 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_21b HBI Conveyor from Reclaim to Enclosed Conveyor 293805.26 4616292.66 585.63 12.6 5.8 2.9 2.45E-02 8.66E-03 5.60E-02 1.98E-02 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_21c HBI Drop from FEL to Hopper 293775.81 4616265.87 585.47 6.6 5.8 1.5 1.44E-02 1.61E-03 3.28E-02 3.67E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_22 HBI Drop from Hopper to Conveyor 293787.59 4616257.10 584.09 6.6 5.8 1.5 1.56E-02 1.75E-03 3.57E-02 3.99E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_26 HBI Loadout Rail Enclosure 293614.68 4616130.60 592.03 5.6 13.5 2.6 7.65E-04 4.33E-04 1.75E-03 9.90E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_27 HBI Loadout Truck Enclosure 293604.50 4616155.25 591.90 55.0 13.5 25.6 3.83E-04 3.83E-04 8.74E-04 5.46E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_29 Feed Recovery Transfer to Stockpile 293756.00 4616382.00 588.85 43.2 16.0 20.1 2.88E-04 2.11E-04 1.90E-03 1.39E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00WE_6 Feed Recovery Stockpile Wind Erosion 293762.00 4616378.00 588.58 43.2 16.0 20.1 1.44E-03 7.19E-04 3.59E-03 1.80E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00FEL_5 Feed Recovery FEL Fugitive 293768.50 4616382.50 588.55 43.2 16.0 20.1 1.84E-03 3.13E-05 1.84E-02 3.13E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_30 Feed Recovery FEL to Hopper 293759.70 4616388.00 588.94 43.2 16.0 20.1 8.47E-03 2.11E-04 5.60E-02 1.39E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00FEL_6 Product Oversize FEL Fugitive 293727.58 4616347.56 587.93 43.2 16.0 20.1 1.84E-03 6.18E-05 1.84E-02 6.18E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00TR_31 Product Oversize FEL to Hopper 293724.40 4616343.90 587.93 43.2 16.0 20.1 8.47E-03 4.22E-04 5.60E-02 2.79E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD1 HBI Haul Road Segment 1 293973.19 4616532.82 587.04 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD2 HBI Haul Road Segment 2 293956.26 4616508.05 587.37 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD3 HBI Haul Road Segment 3 293939.33 4616483.29 588.25 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD4 HBI Haul Road Segment 4 293922.48 4616458.49 587.80 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD5 HBI Haul Road Segment 5 293919.65 4616428.88 586.42 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD6 HBI Haul Road Segment 6 293909.82 4616401.58 583.04 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD7 HBI Haul Road Segment 7 293891.78 4616377.61 583.92 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD8 HBI Haul Road Segment 8 293873.75 4616353.64 585.01 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD9 HBI Haul Road Segment 9 293855.72 4616329.66 585.01 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD10 HBI Haul Road Segment 10 293837.68 4616305.69 585.27 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD11 HBI Haul Road Segment 11 293819.65 4616281.71 584.48 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD12 HBI Haul Road Segment 12 293801.67 4616257.70 583.53 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD13 HBI Haul Road Segment 13 293783.94 4616233.50 583.66 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD14 HBI Haul Road Segment 14 293766.21 4616209.30 583.99 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD15 HBI Haul Road Segment 15 293748.48 4616185.10 587.47 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD16 HBI Haul Road Segment 16 293729.99 4616161.48 587.57 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD17 HBI Haul Road Segment 17 293706.10 4616143.65 589.34 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD18 HBI Haul Road Segment 18 293677.82 4616133.74 591.27 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Potential Emissions (lb/hr)

Page 283: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Volume Source Inputs

Source ID Source Description Easting (m) Northing (m)

Base Elevation

(ft)

Release Height

(ft)Sigma Y

(ft)Sigma Z

(ft) PM25PM-25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO Hexane NH3

Potential Emissions (lb/hr)

HBI_RD19 HBI Haul Road Segment 19 293648.31 4616128.57 586.91 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD20 HBI Haul Road Segment 20 293618.92 4616133.13 591.90 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD21 HBI Haul Road Segment 21 293594.35 4616147.68 591.99 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD22 HBI Haul Road Segment 22 293598.64 4616176.17 591.73 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD23 HBI Haul Road Segment 23 293614.53 4616201.61 591.54 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD24 HBI Haul Road Segment 24 293632.34 4616225.75 588.42 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD25 HBI Haul Road Segment 25 293650.15 4616249.89 588.19 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD26 HBI Haul Road Segment 26 293667.96 4616274.03 587.50 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD27 HBI Haul Road Segment 27 293685.77 4616298.17 587.86 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD28 HBI Haul Road Segment 28 293706.29 4616319.30 587.96 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD29 HBI Haul Road Segment 29 293733.55 4616331.75 588.06 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD30 HBI Haul Road Segment 30 293755.27 4616351.74 587.73 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD31 HBI Haul Road Segment 31 293773.47 4616375.59 588.25 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD32 HBI Haul Road Segment 32 293791.67 4616399.43 588.68 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD33 HBI Haul Road Segment 33 293809.87 4616423.28 588.32 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD34 HBI Haul Road Segment 34 293828.07 4616447.13 588.68 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD35 HBI Haul Road Segment 35 293848.94 4616467.45 588.75 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD36 HBI Haul Road Segment 36 293874.61 4616453.10 588.32 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD37 HBI Haul Road Segment 37 293900.16 4616439.89 587.73 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD38 HBI Haul Road Segment 38 293917.14 4616464.62 588.06 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD39 HBI Haul Road Segment 39 293934.24 4616489.28 588.65 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD40 HBI Haul Road Segment 40 293951.33 4616513.93 587.53 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00HBI_RD41 HBI Haul Road Segment 41 293968.42 4616538.58 587.27 12.8 21.0 11.9 1.03E-03 9.46E-04 4.20E-03 3.85E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD1 Lumps Fines Coating Road Seg 1 293969.38 4616533.84 587.14 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD2 Lumps Fines Coating Road Seg 2 293952.40 4616509.11 587.40 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD3 Lumps Fines Coating Road Seg 3 293935.42 4616484.38 588.55 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD4 Lumps Fines Coating Road Seg 4 293911.86 4616476.79 588.62 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD5 Lumps Fines Coating Road Seg 5 293885.71 4616491.48 588.81 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD6 Lumps Fines Coating Road Seg 6 293858.55 4616503.96 589.17 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD7 Lumps Fines Coating Road Seg 7 293833.12 4616519.27 589.04 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD8 Lumps Fines Coating Road Seg 8 293809.07 4616537.19 588.32 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD9 Lumps Fines Coating Road Seg 9 293785.01 4616555.11 587.93 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD10 Lumps Fines Coating Road Seg 10 293760.95 4616573.03 587.89 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD11 Lumps Fines Coating Road Seg 11 293736.89 4616590.95 588.55 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD12 Lumps Fines Coating Road Seg 12 293712.83 4616608.88 587.73 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD13 Lumps Fines Coating Road Seg 13 293688.78 4616626.80 587.73 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD14 Lumps Fines Coating Road Seg 14 293664.72 4616644.72 587.40 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD15 Lumps Fines Coating Road Seg 15 293636.41 4616648.38 590.52 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD16 Lumps Fines Coating Road Seg 16 293618.49 4616624.32 590.26 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD17 Lumps Fines Coating Road Seg 17 293600.57 4616600.25 590.72 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD18 Lumps Fines Coating Road Seg 18 293582.65 4616576.19 588.68 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD19 Lumps Fines Coating Road Seg 19 293564.73 4616552.13 588.75 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD20 Lumps Fines Coating Road Seg 20 293546.81 4616528.07 589.47 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD21 Lumps Fines Coating Road Seg 21 293528.90 4616504.01 590.22 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00LFC_RD22 Lumps Fines Coating Road Seg 22 293510.98 4616479.95 590.78 12.8 21.0 11.9 6.90E-04 2.62E-04 2.81E-03 1.07E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00REM_RD1 Remet Reclaim Road Segment 1 293698.10 4616307.89 588.06 12.8 21.0 11.9 6.74E-04 1.90E-04 6.74E-03 1.90E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00REM_RD2 Remet Reclaim Road Segment 2 293690.77 4616335.92 587.70 12.8 21.0 11.9 6.74E-04 1.90E-04 6.74E-03 1.90E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00REM_RD3 Remet Reclaim Road Segment 3 293666.72 4616353.85 587.86 12.8 21.0 11.9 6.74E-04 1.90E-04 6.74E-03 1.90E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00REM_RD4 Remet Reclaim Road Segment 4 293642.67 4616371.78 587.93 12.8 21.0 11.9 6.74E-04 1.90E-04 6.74E-03 1.90E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00REM_RD5 Remet Reclaim Road Segment 5 293618.62 4616389.71 587.01 12.8 21.0 11.9 6.74E-04 1.90E-04 6.74E-03 1.90E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00REM_RD6 Remet Reclaim Road Segment 6 293594.57 4616407.64 587.93 12.8 21.0 11.9 6.74E-04 1.90E-04 6.74E-03 1.90E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00REM_RD7 Remet Reclaim Road Segment 7 293570.52 4616425.57 587.70 12.8 21.0 11.9 6.74E-04 1.90E-04 6.74E-03 1.90E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00REM_RD8 Remet Reclaim Road Segment 8 293546.47 4616443.51 589.17 12.8 21.0 11.9 6.74E-04 1.90E-04 6.74E-03 1.90E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00REM_RD9 Remet Reclaim Road Segment 9 293522.41 4616461.44 589.96 12.8 21.0 11.9 6.74E-04 1.90E-04 6.74E-03 1.90E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00

Page 284: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Volume Source Inputs

Source ID Source Description Easting (m) Northing (m)

Base Elevation

(ft)

Release Height

(ft)Sigma Y

(ft)Sigma Z

(ft) PM25PM-25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO Hexane NH3

Potential Emissions (lb/hr)

REM_RD10 Remet Reclaim Road Segment 10 293497.18 4616463.39 589.86 12.8 21.0 11.9 6.74E-04 1.90E-04 6.74E-03 1.90E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00REM_RD11 Remet Reclaim Road Segment 11 293479.06 4616439.52 589.76 12.8 21.0 11.9 6.74E-04 1.90E-04 6.74E-03 1.90E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00REM_RD12 Remet Reclaim Road Segment 12 293466.89 4616423.03 590.62 12.8 21.0 11.9 6.74E-04 1.90E-04 6.74E-03 1.90E-03 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD1 Sludge Road Segment 1 293964.55 4616535.97 587.30 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD2 Sludge Road Segment 2 293947.37 4616511.37 587.73 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD3 Sludge Road Segment 3 293930.19 4616486.78 588.58 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD4 Sludge Road Segment 4 293904.54 4616484.10 588.91 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD5 Sludge Road Segment 5 293878.21 4616498.48 588.94 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD6 Sludge Road Segment 6 293850.94 4616510.47 589.01 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD7 Sludge Road Segment 7 293826.26 4616527.07 588.88 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD8 Sludge Road Segment 8 293802.25 4616545.05 588.29 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD9 Sludge Road Segment 9 293778.23 4616563.03 587.86 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD10 Sludge Road Segment 10 293754.22 4616581.01 588.06 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD11 Sludge Road Segment 11 293730.20 4616598.99 588.39 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD12 Sludge Road Segment 12 293706.12 4616616.87 587.86 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD13 Sludge Road Segment 13 293681.86 4616634.53 587.53 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD14 Sludge Road Segment 14 293657.23 4616651.51 588.09 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD15 Sludge Road Segment 15 293630.61 4616647.38 590.68 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD16 Sludge Road Segment 16 293612.34 4616623.62 590.22 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD17 Sludge Road Segment 17 293594.31 4616599.65 590.85 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD18 Sludge Road Segment 18 293580.39 4616573.88 588.71 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00SLG_RD19 Sludge Road Segment 19 293598.21 4616552.51 588.39 12.8 21.0 11.9 2.14E-04 1.33E-04 8.72E-04 5.41E-04 0.00E+00 0.00E+00 0.00E+00 0.00E+00 0.00E+00PM25 and PM10 - Pollutant names for short-term potential emissions.PM-25 and PM-10 - Pollutant for annual potential emissions.

Page 285: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Point Source Model Input Data (Sources within 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID

Stack Release

Type

FLAT (Non-

Default) Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Stack Height

(ft)Temperature

(°F)

Exit Velocity (ft/sec)

Stack Diameter

(ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE1 TOLEDO SHREDDING LLC (0448011575) 294058.47 4616773.57 590.2 60.0 70. 18.60 3.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE2 TOLEDO SHREDDING LLC (0448011575) 294056.00 4616754.00 590.2 42.0 70. 18.60 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE3 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 10.0 70. 199.04 1.6 0.000 0.000 0.627 0.627 0.000 0.000 0.000 Yes Yes No NoOFFSITE4 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 50.0 70. 449.47 1.5 0.000 0.000 0.627 0.627 0.000 0.000 0.000 Yes Yes No NoOFFSITE5 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 8.0 70. 169.85 1.5 0.000 0.000 0.474 0.474 0.000 0.000 0.000 Yes Yes No NoOFFSITE6 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 50.0 70. 449.47 1.5 0.000 0.000 0.474 0.474 0.000 0.000 0.000 Yes Yes No NoOFFSITE7 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 40.0 70. 0.59 1.9 0.000 0.000 0.040 0.040 0.000 0.000 0.000 Yes Yes No NoOFFSITE8 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 40.0 70. 0.59 1.9 0.000 0.000 0.024 0.024 0.000 0.000 0.000 Yes Yes No NoOFFSITE9 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 8.0 70. 50.00 0.1 0.000 0.000 0.280 0.280 0.000 0.000 0.000 Yes Yes No NoOFFSITE10 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 25.0 70 41.14 6.9 0.000 0.000 0.275 0.275 0.000 0.000 0.000 Yes Yes No NoOFFSITE11 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 95.0 100. 96.32 1.4 0.000 0.000 0.356 0.356 0.000 0.000 0.000 Yes Yes No NoOFFSITE12 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 99.0 100. 127.62 1.8 0.000 0.000 0.356 0.356 0.000 0.000 0.000 Yes Yes No NoOFFSITE13 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 40.0 70. 72.35 1.5 0.000 0.000 0.356 0.356 0.000 0.000 0.000 Yes Yes No NoOFFSITE14 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 40.0 70. 72.35 1.5 0.000 0.000 0.356 0.356 0.000 0.000 0.000 Yes Yes No NoOFFSITE15 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 50.0 70. 50.24 1.8 0.000 0.000 0.356 0.356 0.000 0.000 0.000 Yes Yes No NoOFFSITE16 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 95.0 100. 83.05 1.4 0.000 0.000 0.356 0.356 0.000 0.000 0.000 Yes Yes No NoOFFSITE17 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 95.0 100. 96.32 1.4 0.000 0.000 0.356 0.356 0.000 0.000 0.000 Yes Yes No NoOFFSITE18 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 99.0 100. 127.62 1.8 0.000 0.000 0.356 0.356 0.000 0.000 0.000 Yes Yes No NoOFFSITE19 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 50.0 70. 72.35 1.5 0.000 0.000 0.356 0.356 0.000 0.000 0.000 Yes Yes No NoOFFSITE20 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 50.0 70. 50.24 1.8 0.000 0.000 0.356 0.356 0.000 0.000 0.000 Yes Yes No NoOFFSITE21 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 50.0 70. 41.14 6.9 0.000 0.000 0.130 0.130 0.000 0.000 0.000 Yes Yes No NoOFFSITE22 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 25.0 70. 41.14 6.9 0.000 0.000 0.130 0.130 0.000 0.000 0.000 Yes Yes No NoOFFSITE23 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 25.0 70. 41.14 6.9 0.000 0.000 0.130 0.130 0.000 0.000 0.000 Yes Yes No NoOFFSITE24 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 25.0 70 41.14 6.9 0.000 0.000 2.688 2.688 0.000 0.000 0.000 Yes Yes No NoOFFSITE25 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 25.0 70 41.14 6.9 0.000 0.000 0.928 0.928 0.000 0.000 0.000 Yes Yes No NoOFFSITE26 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 20.0 70. 315.84 1.1 0.000 0.000 2.440 2.440 0.000 0.000 0.000 Yes Yes No NoOFFSITE27 Mondelez Global LLC - Toledo Flour Mill (0448010 291939.00 4615597.00 597.6 25.0 70. 10.00 1.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes No NoOFFSITE28 City of Toledo, Division of Water Reclamation (04 293591.00 4618482.00 576.9 60.0 888 56.01 15.0 0.000 0.000 0.000 0.000 18.000 18.000 29.200 No No Yes YesOFFSITE29 City of Toledo, Division of Water Reclamation (04 293591.00 4618482.00 576.9 60.0 888 65.02 15.0 0.000 0.000 0.000 0.000 12.300 12.300 7.310 No No Yes YesOFFSITE30 City of Toledo, Division of Water Reclamation (04 293659.00 4618249.00 576.9 21.1 358. 62.08 1.4 0.000 0.000 0.000 0.000 0.093 0.093 0.005 No No Yes YesOFFSITE31 City of Toledo, Division of Water Reclamation (04 293659.00 4618249.00 576.9 21.1 358. 62.08 1.4 0.000 0.000 0.000 0.000 6.360 6.360 15.020 No No Yes YesOFFSITE32 City of Toledo, Division of Water Reclamation (04 293659.00 4618249.00 576.9 21.1 358. 62.08 1.4 0.000 0.000 0.000 0.000 6.360 6.360 15.020 No No Yes YesOFFSITE33 Chemtrade Refinery Solutions Limited Partnershi 295618.61 4617346.77 584.0 24.0 480. 75.57 1.9 0.040 0.040 0.040 0.040 0.950 0.950 1.600 Yes Yes Yes YesOFFSITE34 Chemtrade Refinery Solutions Limited Partnershi 295618.61 4617346.77 584.0 24.0 480. 75.57 1.9 0.030 0.030 0.030 0.030 0.830 0.830 1.400 Yes Yes Yes YesOFFSITE35 Chemtrade Refinery Solutions Limited Partnershi 295618.61 4617346.77 584.0 120.0 170. 41.18 3.9 3.226 3.226 4.963 4.963 5.900 5.900 7.410 Yes Yes Yes YesOFFSITE36 Chemtrade Refinery Solutions Limited Partnershi 295618.61 4617346.77 584.0 120.0 170. 23.03 3.9 0.847 0.847 1.304 1.304 3.720 3.720 4.120 Yes Yes Yes YesOFFSITE37 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 150.0 710. 28.31 4.5 1.948 1.948 1.948 1.948 4.533 4.533 3.807 Yes Yes Yes YesOFFSITE38 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 150.0 440. 3.57 16.0 2.200 2.200 2.200 2.200 11.094 11.094 2.292 Yes Yes Yes YesOFFSITE39 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 150.0 440. 3.57 16.0 2.200 2.200 2.200 2.200 13.970 13.970 2.869 Yes Yes Yes YesOFFSITE40 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 120.0 480. 36.45 11.7 5.600 5.600 5.600 5.600 66.702 66.702 25.027 Yes Yes Yes YesOFFSITE41 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 135.0 825. 32.15 4.3 1.440 1.440 1.440 1.440 2.835 2.835 2.382 Yes Yes Yes YesOFFSITE42 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 145.0 460. 15.87 8.5 5.160 5.160 5.160 5.160 60.000 60.000 12.827 Yes Yes Yes YesOFFSITE43 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 120.0 480. 36.45 11.7 1.540 1.540 1.540 1.540 6.992 6.992 5.874 Yes Yes Yes YesOFFSITE44 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 100.0 450. 9.19 3.5 0.170 0.170 0.170 0.170 1.600 1.600 1.880 Yes Yes Yes YesOFFSITE45 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 142.0 500. 13.27 4.0 0.300 0.300 0.300 0.300 4.030 4.030 3.660 Yes Yes Yes YesOFFSITE46 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 120.0 480. 36.45 11.7 0.817 0.817 0.817 0.817 9.100 9.100 9.022 Yes Yes Yes YesOFFSITE47 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 175.0 600. 34.80 6.2 1.249 1.249 1.249 1.249 24.150 24.150 13.800 Yes Yes Yes YesOFFSITE48 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 100.0 520. 4.25 5.0 0.250 0.250 0.250 0.250 0.670 0.670 2.700 Yes Yes Yes YesOFFSITE49 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 101.0 265. 29.27 6.2 2.630 2.630 2.630 2.630 12.710 12.710 38.480 Yes Yes Yes YesOFFSITE50 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 101.0 265. 29.27 6.2 2.630 2.630 2.630 2.630 12.710 12.710 38.480 Yes Yes Yes YesOFFSITE51 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 215.0 265. 16.84 12.3 3.900 3.900 3.900 3.900 23.355 23.355 18.600 Yes Yes Yes YesOFFSITE52 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 48.0 500. 0.67 7.1 0.034 0.034 0.034 0.034 0.441 0.441 0.370 Yes Yes Yes YesOFFSITE53 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 339.0 1620. 30.57 2.5 0.147 0.147 0.147 0.147 1.344 1.344 7.313 Yes Yes Yes YesOFFSITE54 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 336.0 1700. 5.44 2.5 0.485 0.485 0.485 0.485 4.420 4.420 24.050 Yes Yes Yes YesOFFSITE55 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 250.0 400. 46.50 11.0 6.690 6.690 6.690 6.690 40.212 40.212 4.427 Yes Yes Yes YesOFFSITE56 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 125.0 525. 129.09 5.0 6.690 6.690 6.690 6.690 40.212 40.212 4.427 Yes Yes Yes YesOFFSITE57 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 228.0 1170. 38.13 3.5 0.052 0.052 0.052 0.052 0.693 0.693 0.582 Yes Yes Yes YesOFFSITE58 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 175.0 1235. 16.99 5.0 0.600 0.600 0.600 0.600 4.400 4.400 2.700 Yes Yes Yes YesOFFSITE59 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 50.0 100. 0.96 1.0 0.034 0.034 0.034 0.034 0.448 0.448 0.288 Yes Yes Yes YesOFFSITE60 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 175.0 1200. 33.97 0.5 0.055 0.055 0.055 0.055 0.491 0.491 2.671 Yes Yes Yes YesOFFSITE61 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 175.0 1200. 33.97 0.5 0.055 0.055 0.055 0.055 0.491 0.491 2.671 Yes Yes Yes YesOFFSITE62 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 175.0 1200. 39.75 0.5 0.050 0.050 0.050 0.050 0.450 0.450 2.449 Yes Yes Yes YesOFFSITE63 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 215.0 450. 7.37 1.2 0.000 0.000 0.000 0.000 0.001 0.001 0.057 Yes Yes Yes YesOFFSITE64 Oregon Clean Energy - Cooling Tower Cell 1 296389.28 4615758.47 589.8 66 77 27.72 33.0 0.065 0.065 0.065 0.065 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE65 Oregon Clean Energy - Cooling Tower Cell 16 296389.11 4615744.68 589.8 66 77 27.72 33.0 0.065 0.065 0.065 0.065 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE66 Oregon Clean Energy - Cooling Tower Cell 2 296404.77 4615758.47 589.8 66 77 27.72 33.0 0.065 0.065 0.065 0.065 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE67 Oregon Clean Energy - Cooling Tower Cell 15 296404.84 4615744.67 589.8 66 77 27.72 33.0 0.065 0.065 0.065 0.065 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE68 Oregon Clean Energy - Cooling Tower Cell 3 296419.89 4615758.25 589.8 66 77 27.72 33.0 0.065 0.065 0.065 0.065 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE69 Oregon Clean Energy - Cooling Tower Cell 14 296419.90 4615744.35 589.8 66 77 27.72 33.0 0.065 0.065 0.065 0.065 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE70 Oregon Clean Energy - Cooling Tower Cell 4 296435.54 4615758.04 589.8 66 77 27.72 33.0 0.065 0.065 0.065 0.065 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE71 Oregon Clean Energy - Cooling Tower Cell 13 296435.52 4615744.35 589.8 66 77 27.72 33.0 0.065 0.065 0.065 0.065 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE72 Oregon Clean Energy - Cooling Tower Cell 5 296451.20 4615758.15 589.8 66 77 27.72 33.0 0.065 0.065 0.065 0.065 0.000 0.000 0.000 Yes Yes Yes Yes

Page 286: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Point Source Model Input Data (Sources within 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID

Stack Release

Type

FLAT (Non-

Default) Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Stack Height

(ft)Temperature

(°F)

Exit Velocity (ft/sec)

Stack Diameter

(ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE73 Oregon Clean Energy - Cooling Tower Cell 12 296451.20 4615744.35 589.8 66 77 27.72 33.0 0.065 0.065 0.065 0.065 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE74 Oregon Clean Energy - Cooling Tower Cell 6 296466.87 4615758.15 589.8 66 77 27.72 33.0 0.065 0.065 0.065 0.065 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE75 Oregon Clean Energy - Cooling Tower Cell 11 296466.87 4615744.35 589.8 66 77 27.72 33.0 0.065 0.065 0.065 0.065 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE76 Oregon Clean Energy - Cooling Tower Cell 7 296482.55 4615758.09 589.8 66 77 27.72 33.0 0.065 0.065 0.065 0.065 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE77 Oregon Clean Energy - Cooling Tower Cell 10 296482.37 4615744.40 589.8 66 77 27.72 33.0 0.065 0.065 0.065 0.065 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE78 Oregon Clean Energy - Cooling Tower Cell 8 296498.15 4615758.09 589.8 66 77 27.72 33.0 0.065 0.065 0.065 0.065 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE79 Oregon Clean Energy - Cooling Tower Cell 9 296498.16 4615744.46 589.8 66 77 27.72 33.0 0.065 0.065 0.065 0.065 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE80 Oregon Clean Energy - HRGN 296560.98 4615757.31 589.8 240 176 53.30 22.0 13.401 13.401 13.401 13.401 19.982 19.982 19.982 Yes Yes Yes YesOFFSITE81 Oregon Clean Energy - Aux Boiler 296560.98 4615757.00 589.8 240 200 16.75 4.0 0.000 0.000 0.000 0.000 0.000 0.000 1.982 Yes Yes Yes YesOFFSITE82 Oregon Clean Energy - HRGS 296560.71 4615714.43 589.8 240 176 53.30 22.0 13.401 13.401 13.401 13.401 19.982 19.982 19.982 Yes Yes Yes YesOFFSITE82a Oregon Energy Center-Turbine 1 297092.82 4615514.53 591.0 185 165 68.42 21.0 14.900 14.900 14.900 14.900 24.300 24.300 14.900 Yes Yes Yes YesOFFSITE82b Oregon Energy Center-Turbine 2 297092.75 4615560.13 591.0 185 165 68.42 21.0 14.900 14.900 14.900 14.900 24.300 24.300 14.900 Yes Yes Yes YesOFFSITE82c Oregon Energy Center-Aux Boiler 297092.83 4615510.44 591.0 185 340 37.11 2.5 0.300 0.300 0.300 0.300 0.760 0.760 2.080 Yes Yes Yes YesOFFSITE82d Oregon Energy Center-Cooling Tower Cell 1 297065.11 4615415.73 591.0 43.5105 -475 24.24 35.6 0.036 0.036 0.093 0.093 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE82e Oregon Energy Center-Cooling Tower Cell 2 297077.19 4615427.69 591.0 43.5105 -475 24.24 35.6 0.036 0.036 0.093 0.093 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE82f Oregon Energy Center-Cooling Tower Cell 3 297089.37 4615439.78 591.0 43.5105 -475 24.24 35.6 0.036 0.036 0.093 0.093 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE82g Oregon Energy Center-Cooling Tower Cell 4 297101.40 4615451.85 591.0 43.5105 -475 24.24 35.6 0.036 0.036 0.093 0.093 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE82h Oregon Energy Center-Cooling Tower Cell 5 297113.35 4615463.88 591.0 43.5105 -475 24.24 35.6 0.036 0.036 0.093 0.093 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE82i Oregon Energy Center-Cooling Tower Cell 6 297125.42 4615475.82 591.0 43.5105 -475 24.24 35.6 0.036 0.036 0.093 0.093 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE82j Oregon Energy Center-Cooling Tower Cell 7 297137.62 4615488.19 591.0 43.5105 -475 24.24 35.6 0.036 0.036 0.093 0.093 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE82k Oregon Energy Center-Cooling Tower Cell 8 297149.52 4615500.22 591.0 43.5105 -475 24.24 35.6 0.036 0.036 0.093 0.093 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE82l Oregon Energy Center-Cooling Tower Cell 9 297161.65 4615512.27 591.0 43.5105 -475 24.24 35.6 0.036 0.036 0.093 0.093 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE82m Oregon Energy Center-Cooling Tower Cell 10 297173.78 4615524.40 591.0 43.5105 -475 24.24 35.6 0.036 0.036 0.093 0.093 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE82n Oregon Energy Center-Emergency Engine 297058.78 4615459.17 591.0 12.5984 910 202.37 1.0 0.500 0.500 0.500 0.500 16.100 16.100 8.800 Yes Yes Yes YesOFFSITE82o Oregon Energy Center-Fire Water Pump 297113.78 4615522.08 591.0 13.5007 961 118.83 0.5 0.100 0.100 0.100 0.100 1.970 1.970 1.730 Yes Yes Yes YesOFFSITE83 Libbey Glass Inc. (0448010066) 290501.14 4616234.53 592.6 51.0 390. 43.68 1.3 0.206 0.206 0.206 0.206 1.494 1.494 0.927 Yes Yes Yes YesOFFSITE84 Libbey Glass Inc. (0448010066) 290494.38 4616241.29 592.6 51.0 390. 43.68 1.3 0.206 0.206 0.206 0.206 1.494 1.494 0.927 Yes Yes Yes YesOFFSITE85 Libbey Glass Inc. (0448010066) 290436.39 4616294.93 592.6 61.0 390. 43.68 1.3 0.206 0.206 0.206 0.206 1.494 1.494 0.927 Yes Yes Yes YesOFFSITE86 Libbey Glass Inc. (0448010066) 290467.32 4616323.45 592.6 100.0 651. 12.74 5.0 2.680 2.680 3.400 3.400 15.411 15.411 0.022 Yes Yes Yes YesOFFSITE87 Libbey Glass Inc. (0448010066) 290458.62 4616333.59 592.6 65.0 651. 50.96 2.5 2.240 2.240 8.400 8.400 8.928 8.928 0.013 Yes Yes Yes YesOFFSITE88 Libbey Glass Inc. (0448010066) 290449.43 4616342.29 592.6 125.0 651. 17.04 5.8 2.430 2.430 6.300 6.300 46.300 46.300 1.067 Yes Yes Yes YesOFFSITE89 Libbey Glass Inc. (0448010066) 290400.63 4616379.50 592.6 40.0 200. 34.95 1.7 0.000 0.000 0.027 0.027 1.005 1.005 0.301 Yes Yes Yes YesOFFSITE90 Libbey Glass Inc. (0448010066) 290476.50 4616315.23 592.6 65.0 200. 69.22 2.5 1.670 1.670 8.660 8.660 28.000 28.000 0.750 Yes Yes Yes YesOFFSITE91 Libbey Glass Inc. (0448010066) 290418.99 4616397.40 592.6 76.0 80. 131.60 2.2 0.000 0.000 5.500 5.500 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE92 MARATHON PETROLEUM CO LP (0448020033) 296126.59 4614028.58 597.5 40.0 1300. 1.97 8.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE93 FirstEnergy Generation LLC, Bay Shore Plant (044 297155.93 4618506.56 580.9 300.0 303. 80.9 12.0 11.340 11.340 11.340 11.340 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE94 FirstEnergy Generation LLC, Bay Shore Plant (044 297155.93 4618506.56 580.9 300.0 303. 80.94 12.0 44.378 44.378 60.331 60.331 529.300 529.300 352.800 Yes Yes Yes YesOFFSITE95 FirstEnergy Generation LLC, Bay Shore Plant (044 297155.93 4618506.56 580.9 110.0 83. 3.41 3.3 0.029 0.029 0.029 0.029 1.740 1.740 0.114 Yes Yes Yes YesOFFSITE96 FirstEnergy Generation LLC, Bay Shore Plant (044 297155.93 4618506.56 580.9 110.0 83. 3.41 3.3 0.186 0.186 2.018 2.018 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE97 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.600 1.600 2.711 No No Yes YesOFFSITE98 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.600 1.600 2.711 No No Yes YesOFFSITE99 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.600 1.600 2.711 No No Yes YesOFFSITE100 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.202 1.202 0.240 No No Yes YesOFFSITE101 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.503 1.503 0.301 No No Yes YesOFFSITE102 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.503 1.503 0.301 No No Yes YesOFFSITE103 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.202 1.202 0.240 No No Yes YesOFFSITE104 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.503 1.503 0.301 No No Yes YesOFFSITE105 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.202 1.202 0.240 No No Yes YesOFFSITE106 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.202 1.202 0.240 No No Yes YesOFFSITE107 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.353 1.353 0.541 No No Yes YesOFFSITE108 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.202 1.202 0.240 No No Yes YesOFFSITE109 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.052 1.052 0.210 No No Yes YesOFFSITE110 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.353 1.353 0.271 No No Yes YesOFFSITE111 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.052 1.052 0.210 No No Yes YesOFFSITE112 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.503 1.503 0.301 No No Yes YesOFFSITE113 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.503 1.503 0.301 No No Yes YesOFFSITE114 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.503 1.503 0.301 No No Yes YesOFFSITE115 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.353 1.353 0.271 No No Yes YesOFFSITE116 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.353 1.353 0.271 No No Yes YesOFFSITE117 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.202 1.202 0.240 No No Yes YesOFFSITE118 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.653 1.653 0.331 No No Yes YesOFFSITE119 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.103 1.103 0.221 No No Yes YesOFFSITE120 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 1.202 1.202 0.240 No No Yes YesOFFSITE121 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 34.0 100. 104.18 1.5 0.000 0.000 0.000 0.000 8.100 8.100 7.900 No No Yes YesOFFSITE122 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 90.0 150. 52.87 5.7 0.000 0.000 0.000 0.000 0.524 0.524 0.435 No No Yes YesOFFSITE123 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 135.0 150. 22.06 1.2 0.000 0.000 0.000 0.000 4.180 4.180 3.469 No No Yes YesOFFSITE124 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 135.0 150. 40.79 3.3 0.000 0.000 0.000 0.000 4.180 4.180 3.469 No No Yes YesOFFSITE125 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 135.0 70. 42.26 4.7 0.000 0.000 0.000 0.000 4.180 4.180 3.469 No No Yes YesOFFSITE126 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 135.0 70. 44.01 3.3 0.000 0.000 0.000 0.000 4.180 4.180 3.469 No No Yes YesOFFSITE127 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 135.0 150. 8.48 1.2 0.000 0.000 0.000 0.000 4.180 4.180 3.469 No No Yes YesOFFSITE128 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 90.0 150. 52.87 5.7 0.000 0.000 0.000 0.000 5.040 5.040 4.180 No No Yes YesOFFSITE129 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 90.3 150. 43.25 4.7 0.000 0.000 0.000 0.000 1.200 1.200 0.996 No No Yes Yes

Page 287: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Point Source Model Input Data (Sources within 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID

Stack Release

Type

FLAT (Non-

Default) Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Stack Height

(ft)Temperature

(°F)

Exit Velocity (ft/sec)

Stack Diameter

(ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE130 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 119.0 285. 25.48 2.0 0.000 0.000 0.000 0.000 1.200 1.200 0.996 No No Yes YesOFFSITE131 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 190.0 70. 47.48 7.4 0.000 0.000 0.000 0.000 5.040 5.040 4.180 No No Yes YesOFFSITE132 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 190.0 70. 47.48 7.4 0.000 0.000 0.000 0.000 5.040 5.040 4.180 No No Yes YesOFFSITE133 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 190.0 70. 41.37 6.8 0.000 0.000 0.000 0.000 5.040 5.040 4.180 No No Yes YesOFFSITE134 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 190.0 70. 41.37 6.8 0.000 0.000 0.000 0.000 5.040 5.040 4.180 No No Yes YesOFFSITE135 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 135.0 145. 49.81 2.5 0.000 0.000 0.000 0.000 5.040 5.040 4.180 No No Yes YesOFFSITE136 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 5.0 70 1.00 1.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE137 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 5.0 70 1.00 1.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE138 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 5.0 70 1.00 1.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE139 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 5.0 70 1.00 1.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE140 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 5.0 70 1.00 1.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE141 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 135.0 70. 45.12 4.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE142 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 82.0 70. 38.47 3.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE143 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 82.0 70. 41.33 3.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE144 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 72.0 70. 43.06 2.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE145 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 72.0 70. 44.22 3.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE146 FCA US LLC - Toledo North Assembly (044801041 290346.00 4619298.00 591.5 72.0 70. 42.61 3.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE147 Hoffman Road Landfill (0448011576) 291397.63 4620215.51 587.7 30.7 30. 1.10 4.6 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE148 FCA US LLC- Wrangler Paint Facility (0448011731 289907.00 4618807.00 591.1 77.0 325. 15.72 3.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE149 FCA US LLC- Wrangler Paint Facility (0448011731 289907.00 4618807.00 591.1 77.0 270. 42.07 6.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE150 FCA US LLC- Wrangler Paint Facility (0448011731 289907.00 4618807.00 591.1 104.8 75. 50.56 4.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE151 FCA US LLC- Wrangler Paint Facility (0448011731 289907.00 4618807.00 591.1 77.0 270. 42.07 6.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE152 FCA US LLC- Wrangler Paint Facility (0448011731 289907.00 4618807.00 591.1 104.8 70. 50.51 3.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE153 FCA US LLC- Wrangler Paint Facility (0448011731 289907.00 4618807.00 591.1 104.8 80. 52.15 5.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE154 FCA US LLC- Wrangler Paint Facility (0448011731 289907.00 4618807.00 591.1 104.8 80. 50.33 4.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE155 Crown Cork & Seal (0448010466) 290618.46 4620453.84 588.3 55.0 550. 69.59 3.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE156 Crown Cork & Seal (0448010466) 290618.46 4620453.84 588.3 55.0 725. 51.15 4.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE157 ST. VINCENT MERCY MEDICAL CENTER (04480100 288221.52 4616049.03 608.7 150.0 436. 27.68 3.4 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE158 ST. VINCENT MERCY MEDICAL CENTER (04480100 288221.52 4616049.03 608.7 150.0 436. 27.68 3.4 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE159 Perstorp Polyols, Inc. (0448010133) 289343.00 4619943.00 592.2 50.0 280. 40.76 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE160 Perstorp Polyols, Inc. (0448010133) 289343.00 4619943.00 592.2 107.5 230. 60.51 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE161 Perstorp Polyols, Inc. (0448010133) 289343.00 4619943.00 592.2 24.0 30. 0.20 0.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE162 Perstorp Polyols, Inc. (0448010133) 289343.00 4619943.00 592.2 26.0 120. 0.20 0.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE163 Perstorp Polyols, Inc. (0448010133) 289343.00 4619943.00 592.2 8.0 70. 12.74 0.1 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE164 Perstorp Polyols, Inc. (0448010133) 289343.00 4619943.00 592.2 10.0 120. 0.20 0.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE165 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 88.3 700. 22.93 5.0 1.300 1.300 1.300 1.300 4.865 4.865 4.087 Yes Yes Yes YesOFFSITE166 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 88.3 700. 22.93 5.0 1.300 1.300 1.300 1.300 4.636 4.636 3.895 Yes Yes Yes YesOFFSITE167 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 88.3 700. 22.93 5.0 1.300 1.300 1.300 1.300 5.138 5.138 4.316 Yes Yes Yes YesOFFSITE168 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 125.0 950. 33.11 6.2 2.300 2.300 2.300 2.300 29.135 29.135 8.740 Yes Yes Yes YesOFFSITE169 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 52.0 600. 10.99 4.7 1.260 1.260 1.260 1.260 2.520 2.520 1.271 Yes Yes Yes YesOFFSITE170 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 52.0 600. 10.99 4.7 1.260 1.260 1.260 1.260 2.520 2.520 1.338 Yes Yes Yes YesOFFSITE171 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 59.0 715. 13.30 5.0 1.520 1.520 1.520 1.520 3.040 3.040 2.171 Yes Yes Yes YesOFFSITE172 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 63.0 740. 23.29 4.0 0.840 0.840 0.840 0.840 2.345 2.345 1.970 Yes Yes Yes YesOFFSITE173 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 120.0 416. 271.29 1.8 2.160 2.160 2.160 2.160 4.320 4.320 6.877 Yes Yes Yes YesOFFSITE174 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 90.0 740. 29.43 4.0 1.400 1.400 1.400 1.400 5.200 5.200 4.369 Yes Yes Yes YesOFFSITE175 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 47.0 502. 25.98 2.8 0.560 0.560 0.560 0.560 1.120 1.120 0.660 Yes Yes Yes YesOFFSITE176 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 5.0 70.0 1.0 1.0 2.520 2.520 2.520 2.520 5.040 5.040 10.376 Yes Yes Yes YesOFFSITE177 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 140.0 860. 38.37 4.8 1.600 1.600 1.600 1.600 3.417 3.417 2.871 Yes Yes Yes YesOFFSITE178 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 140.0 820. 33.42 4.8 1.420 1.420 1.420 1.420 3.884 3.884 3.263 Yes Yes Yes YesOFFSITE179 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 140.0 780. 13.58 5.5 0.540 0.540 0.540 0.540 1.351 1.351 1.135 Yes Yes Yes YesOFFSITE180 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 140.0 760. 23.04 5.2 1.240 1.240 1.240 1.240 2.491 2.491 2.093 Yes Yes Yes YesOFFSITE181 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 140.0 585. 22.95 5.8 1.740 1.740 1.740 1.740 6.646 6.646 5.583 Yes Yes Yes YesOFFSITE182 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 140.0 585. 22.95 5.8 1.740 1.740 1.740 1.740 6.646 6.646 5.583 Yes Yes Yes YesOFFSITE183 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 175.0 500. 18.18 12.0 2.400 2.400 2.400 2.400 26.300 26.300 7.890 Yes Yes Yes YesOFFSITE184 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 175.0 500. 18.18 12.0 4.340 4.340 4.340 4.340 46.563 46.563 13.969 Yes Yes Yes YesOFFSITE185 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 140.0 545. 23.11 6.7 1.280 1.280 1.280 1.280 5.096 5.096 4.280 Yes Yes Yes YesOFFSITE186 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 140.0 545. 23.11 6.7 0.840 0.840 0.840 0.840 2.893 2.893 2.431 Yes Yes Yes YesOFFSITE187 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 100.0 420. 12.31 5.0 0.860 0.860 0.860 0.860 2.632 2.632 2.206 Yes Yes Yes YesOFFSITE188 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 172.0 535. 7.46 8.7 0.340 0.340 0.340 0.340 8.160 8.160 2.240 Yes Yes Yes YesOFFSITE189 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 175.0 290. 29.99 7.1 1.860 1.860 1.860 1.860 30.000 30.000 20.590 Yes Yes Yes YesOFFSITE190 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 5.0 70.0 1.0 1.0 0.148 0.148 0.148 0.148 0.296 0.296 0.000 Yes Yes Yes YesOFFSITE191 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 159.0 650. 19.81 6.0 1.940 1.940 1.940 1.940 4.170 4.170 8.580 Yes Yes Yes YesOFFSITE192 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 124.0 482. 18.91 3.6 1.060 1.060 1.060 1.060 2.280 2.280 4.690 Yes Yes Yes YesOFFSITE193 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 151.0 615. 22.12 3.7 0.310 0.310 0.310 0.310 1.600 1.600 3.290 Yes Yes Yes YesOFFSITE194 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 62.0 350. 20.98 4.7 0.374 0.374 0.374 0.374 2.006 2.006 4.130 Yes Yes Yes YesOFFSITE195 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 62.0 350. 20.98 4.7 0.353 0.353 0.353 0.353 1.893 1.893 3.897 Yes Yes Yes YesOFFSITE196 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 275.0 2000. 254.78 3.5 0.838 0.838 0.838 0.838 6.459 6.459 33.632 Yes Yes Yes YesOFFSITE197 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 243.0 2000. 268.37 2.5 15.870 15.870 15.870 15.870 3.445 3.445 17.581 Yes Yes Yes YesOFFSITE198 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 199.0 140. 82.65 10.2 75.780 75.780 75.780 75.780 45.300 45.300 62.135 Yes Yes Yes YesOFFSITE199 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 150.0 1140. 35.22 3.6 0.560 0.560 0.560 0.560 0.752 0.752 1.507 Yes Yes Yes YesOFFSITE200 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 22.0 400. 26.38 1.3 0.084 0.084 0.084 0.084 11.817 11.817 1.660 Yes Yes Yes YesOFFSITE201 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 22.0 400. 26.38 1.3 0.084 0.084 0.084 0.084 11.817 11.817 1.660 Yes Yes Yes Yes

Page 288: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Point Source Model Input Data (Sources within 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID

Stack Release

Type

FLAT (Non-

Default) Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Stack Height

(ft)Temperature

(°F)

Exit Velocity (ft/sec)

Stack Diameter

(ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE202 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 5.0 70.0 1.0 1.0 0.120 0.120 0.120 0.120 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE203 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 150.0 1350. 29.58 3.9 1.360 1.360 1.360 1.360 2.550 2.550 5.110 Yes Yes Yes YesOFFSITE204 NORTH TOLEDO GRAPHICS LLC (0448010300) 288040.96 4620900.87 595.5 56.0 230. 0.10 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE205 NORTH TOLEDO GRAPHICS LLC (0448010300) 288040.96 4620900.87 595.5 58.4 230. 0.16 1.6 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE206 NORTH TOLEDO GRAPHICS LLC (0448010300) 288040.96 4620900.87 595.5 56.0 230. 0.10 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE207 NORTH TOLEDO GRAPHICS LLC (0448010300) 288040.96 4620900.87 595.5 58.4 230. 0.16 1.6 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE208 NORTH TOLEDO GRAPHICS LLC (0448010300) 288040.96 4620900.87 595.5 56.0 230. 0.10 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE209 NORTH TOLEDO GRAPHICS LLC (0448010300) 288040.96 4620900.87 595.5 58.4 230. 0.16 1.6 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE210 NORTH TOLEDO GRAPHICS LLC (0448010300) 288040.96 4620900.87 595.5 58.4 230. 0.16 1.6 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE211 NORTH TOLEDO GRAPHICS LLC (0448010300) 288040.96 4620900.87 595.5 26.0 694. 15.64 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE212 TRANSFLO Terminal Services, Inc. (0448011937) 289109.24 4611009.76 594.3 10.0 70.0 21.66 1.4 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE213 Evergreen Recycling and Disposal Facility (038700 292522.11 4608668.92 612.1 20.0 1064. 1150.74 1.0 0.000 0.000 2.460 2.460 0.000 0.000 53.500 No Yes No YesOFFSITE214 Tembec BTLSR Inc (0448010370) 285785.00 4615442.00 614.5 50.0 200. 2.86 3.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE215 Tembec BTLSR Inc (0448010370) 285785.00 4615442.00 614.5 50.0 200. 2.86 3.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE216 Tembec BTLSR Inc (0448010370) 285785.00 4615442.00 614.5 42.0 110. 50.25 3.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE217 Tembec BTLSR Inc (0448010370) 285785.00 4615442.00 614.5 50.0 110. 18.09 5.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE218 Tembec BTLSR Inc (0448010370) 285785.00 4615442.00 614.5 35.0 110. 50.72 3.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE219 Tembec BTLSR Inc (0448010370) 285785.00 4615442.00 614.5 8.0 155. 371.55 0.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE220 Tembec BTLSR Inc (0448010370) 285785.00 4615442.00 614.5 5.0 70.0 1.0 1.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE221 MSC Walbridge Coatings Inc (0387000046) 290892.00 4608407.21 614.5 30.0 265. 27.07 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE222 MSC Walbridge Coatings Inc (0387000046) 290892.00 4608407.21 614.5 30.0 390. 23.59 1.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE223 MSC Walbridge Coatings Inc (0387000046) 290892.00 4608407.21 614.5 30.0 265. 27.07 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE224 MSC Walbridge Coatings Inc (0387000046) 290892.00 4608407.21 614.5 50.0 275. 46.00 6.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE225 MSC Walbridge Coatings Inc (0387000046) 290892.00 4608407.21 614.5 50.0 275. 46.00 6.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE226 MSC Walbridge Coatings Inc (0387000046) 290892.00 4608407.21 614.5 30.0 85. 41.14 4.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE227 General Motors LLC - Toledo (0448010404) 285507.31 4622025.46 608.7 51.0 200. 21.49 3.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE228 General Motors LLC - Toledo (0448010404) 285507.31 4622025.46 608.7 51.0 200. 10.53 5.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE229 General Motors LLC - Toledo (0448010404) 285507.31 4622025.46 608.7 51.0 200. 10.53 5.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE230 Pilkington North America Inc (0487010012) 286571.12 4609416.64 610.1 44.0 395. 18.59 1.3 0.025 0.025 0.033 0.033 0.434 0.434 0.365 Yes Yes Yes YesOFFSITE231 Pilkington North America Inc (0487010012) 286571.12 4609416.64 610.1 44.0 395. 18.59 1.3 0.019 0.019 0.025 0.025 0.329 0.329 0.276 Yes Yes Yes YesOFFSITE232 Pilkington North America Inc (0487010012) 286571.12 4609416.64 610.1 44.0 395. 18.59 1.3 0.019 0.019 0.025 0.025 0.329 0.329 0.276 Yes Yes Yes YesOFFSITE233 Pilkington North America Inc (0487010012) 286571.12 4609416.64 610.1 44.0 1400. 8.63 4.0 6.241 6.241 6.553 6.553 13.153 13.153 0.031 Yes Yes Yes YesOFFSITE234 Pilkington North America Inc (0487010012) 286571.12 4609416.64 610.1 44.0 400. 8.63 4.0 6.241 6.241 6.553 6.553 13.153 13.153 0.031 Yes Yes Yes YesOFFSITE235 Pilkington North America Inc (0487010012) 286571.12 4609416.64 610.1 44.0 1200. 30.12 8.0 6.241 6.241 6.553 6.553 13.153 13.153 0.031 Yes Yes Yes YesOFFSITE236 Pilkington North America Inc (0487010012) 286571.12 4609416.64 610.1 44.0 1310. 40.68 8.0 41.000 41.000 41.000 41.000 220.000 220.000 200.000 Yes Yes Yes YesOFFSITE237 Pilkington North America Inc (0487010012) 286571.12 4609416.64 610.1 5.0 70.0 1.0 1.0 0.300 0.300 39.800 39.800 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE238 Pilkington North America Inc (0487010012) 286571.12 4609416.64 610.1 5.0 70.0 1.0 1.0 0.440 0.440 0.440 0.440 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE239 Pilkington North America Inc (0487010012) 286571.12 4609416.64 610.1 5.0 70.0 1.0 1.0 0.873 0.873 9.090 9.090 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE240 Pilkington North America Inc (0487010012) 286571.12 4609416.64 610.1 5.0 70.0 1.0 1.0 3.783 3.783 23.430 23.430 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE241 Pilkington North America Inc (0487010012) 286571.12 4609416.64 610.1 5.0 70.0 1.0 1.0 0.873 0.873 10.500 10.500 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE242 Pilkington North America Inc (0487010012) 286571.12 4609416.64 610.1 5.0 70.0 1.0 1.0 3.380 3.380 27.100 27.100 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE243 Pilkington North America Inc (0487010012) 286571.12 4609416.64 610.1 5.0 70.0 1.0 1.0 1.000 1.000 1.000 1.000 10.000 10.000 3.100 Yes Yes Yes YesOFFSITE244 Pilkington North America Inc (0487010012) 286571.12 4609416.64 610.1 5.0 70.0 1.0 1.0 1.000 1.000 1.000 1.000 10.000 10.000 3.100 Yes Yes Yes YesOFFSITE245 Pilkington North America Inc (0487010012) 286571.12 4609416.64 610.1 5.0 70.0 1.0 1.0 1.000 1.000 1.000 1.000 10.000 10.000 3.100 Yes Yes Yes YesOFFSITE246 BOWERS ASPHALT & PAVING, INC (0387040084) 290422.06 4607017.37 618.0 14.0 617. 974.05 0.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE247 BOWERS ASPHALT & PAVING, INC (0387040084) 290422.06 4607017.37 618.0 32.0 270. 211.73 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE248 Norplas Industries Inc. (0387000362) 287960.55 4607998.59 622.6 69.2 319. 19.11 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE249 Norplas Industries Inc. (0387000362) 287960.55 4607998.59 622.6 69.2 375. 15.59 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE250 Norplas Industries Inc. (0387000362) 287960.55 4607998.59 622.6 69.2 375. 15.59 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE251 Norplas Industries Inc. (0387000362) 287960.55 4607998.59 622.6 69.2 375. 12.57 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE252 Norplas Industries Inc. (0387000362) 287960.55 4607998.59 622.6 69.2 200. 34.95 2.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE253 Norplas Industries Inc. (0387000362) 287960.55 4607998.59 622.6 69.2 75. 29.97 2.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE254 Norplas Industries Inc. (0387000362) 287960.55 4607998.59 622.6 72.2 75. 16.12 3.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE255 Norplas Industries Inc. (0387000362) 287960.55 4607998.59 622.6 78.1 300. 27.38 7.1 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE256 Norplas Industries Inc. (0387000362) 287960.55 4607998.59 622.6 69.2 70. 37.74 1.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE257 SHELLY MATERIALS PLANT # 4132 (0448010386) 283209.00 4614406.00 619.6 38.0 280. 87.73 3.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE258 UNIVERSITY OF TOLEDO - MAIN CAMPUS (04480 282369.20 4615420.75 596.9 98.0 314. 6.24 3.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE259 UNIVERSITY OF TOLEDO - MAIN CAMPUS (04480 282369.20 4615420.75 596.9 98.0 300. 44.36 5.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE260 UNIVERSITY OF TOLEDO - MAIN CAMPUS (04480 282369.20 4615420.75 596.9 98.0 300. 44.36 5.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE261 UNIVERSITY OF TOLEDO - MAIN CAMPUS (04480 282369.20 4615420.75 596.9 98.0 300. 44.36 5.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE262 UNIVERSITY OF TOLEDO - MAIN CAMPUS (04480 282369.20 4615420.75 596.9 98.0 300. 44.36 5.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE263 UNIVERSITY OF TOLEDO - MAIN CAMPUS (04480 282369.20 4615420.75 596.9 98.0 300. 44.36 5.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE264 UNIVERSITY OF TOLEDO - MAIN CAMPUS (04480 282369.20 4615420.75 596.9 98.0 300. 44.36 5.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE265 UNIVERSITY OF TOLEDO - MAIN CAMPUS (04480 282369.20 4615420.75 596.9 98.0 300. 44.36 5.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE266 UNIVERSITY OF TOLEDO - MAIN CAMPUS (04480 282369.20 4615420.75 596.9 98.0 300. 44.36 5.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE267 Calphalon Group, Newell - Rubbermaid, Inc. (038 288017.61 4606623.33 621.0 40.0 500. 21.93 2.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE268 Calphalon Group, Newell - Rubbermaid, Inc. (038 288017.61 4606623.33 621.0 40.0 500. 42.46 1.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE269 Calphalon Group, Newell - Rubbermaid, Inc. (038 288017.61 4606623.33 621.0 40.0 500. 29.49 1.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE270 Calphalon Group, Newell - Rubbermaid, Inc. (038 288017.61 4606623.33 621.0 40.0 500. 21.93 2.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE271 Calphalon Group, Newell - Rubbermaid, Inc. (038 288017.61 4606623.33 621.0 40.0 500. 42.46 1.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE272 Calphalon Group, Newell - Rubbermaid, Inc. (038 288017.61 4606623.33 621.0 40.0 500. 29.49 1.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE273 American Warming and Ventilating, a division of 298550.42 4606336.13 607.3 28.0 70. 4.78 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No No

Page 289: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Point Source Model Input Data (Sources within 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID

Stack Release

Type

FLAT (Non-

Default) Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Stack Height

(ft)Temperature

(°F)

Exit Velocity (ft/sec)

Stack Diameter

(ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE274 American Warming and Ventilating, a division of 298550.42 4606336.13 607.3 28.0 500. 5.84 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE275 American Warming and Ventilating, a division of 298550.42 4606336.13 607.3 22.0 70. 37.44 3.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE276 American Warming and Ventilating, a division of 298550.42 4606336.13 607.3 22.0 70. 37.44 3.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE277 American Warming and Ventilating, a division of 298550.42 4606336.13 607.3 28.0 70. 33.03 3.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE278 American Warming and Ventilating, a division of 298550.42 4606336.13 607.3 28.0 70. 33.03 3.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE279 American Warming and Ventilating, a division of 298550.42 4606336.13 607.3 28.0 70. 1.65 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE280 American Warming and Ventilating, a division of 298550.42 4606336.13 607.3 28.0 500. 5.84 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE281 Decorative Panels International Inc (0448011193) 282413.86 4613073.27 623.9 48.0 300. 10.09 2.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE282 Decorative Panels International Inc (0448011193) 282413.86 4613073.27 623.9 48.0 450. 32.02 2.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE283 Decorative Panels International Inc (0448011193) 282413.86 4613073.27 623.9 48.0 370. 32.02 2.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE284 Decorative Panels International Inc (0448011193) 282413.86 4613073.27 623.9 37.0 1150. 8.29 3.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE285 University of Toledo Health Science Campus (044 282093.37 4610891.36 624.9 135.0 362. 34.42 2.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE286 University of Toledo Health Science Campus (044 282093.37 4610891.36 624.9 135.0 362. 34.42 2.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE287 University of Toledo Health Science Campus (044 282093.37 4610891.36 624.9 135.0 362. 34.42 2.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE288 University of Toledo Health Science Campus (044 282093.37 4610891.36 624.9 135.0 362. 34.42 2.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE289 University of Toledo Health Science Campus (044 282093.37 4610891.36 624.9 135.0 362. 34.42 2.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE290 University of Toledo Health Science Campus (044 282093.37 4610891.36 624.9 135.0 362. 34.42 2.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE291 University of Toledo Health Science Campus (044 282093.37 4610891.36 624.9 38.5 617. 74.12 2.9 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE292 University of Toledo Health Science Campus (044 282093.37 4610891.36 624.9 135.0 520. 318.47 0.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE293 University of Toledo Health Science Campus (044 282093.37 4610891.36 624.9 135.0 520. 318.47 0.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE294 University of Toledo Health Science Campus (044 282093.37 4610891.36 624.9 3.5 520. 120.60 1.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE295 University of Toledo Health Science Campus (044 282093.37 4610891.36 624.9 38.5 798. 0.42 2.9 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE296 HA INTERNATIONAL LLC (0448011215) 280600.63 4610565.60 592.3 32.0 70. 37.74 1.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE297 HA INTERNATIONAL LLC (0448011215) 280600.63 4610565.60 592.3 32.0 70. 37.74 1.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE298 HA INTERNATIONAL LLC (0448011215) 280600.63 4610565.60 592.3 32.0 70. 37.74 1.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE299 HA INTERNATIONAL LLC (0448011215) 280600.63 4610565.60 592.3 32.0 70. 59.45 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE300 HA INTERNATIONAL LLC (0448011215) 280600.63 4610565.60 592.3 32.0 70. 59.45 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE301 HA INTERNATIONAL LLC (0448011215) 280600.63 4610565.60 592.3 32.0 70. 59.45 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE302 HA INTERNATIONAL LLC (0448011215) 280600.63 4610565.60 592.3 32.0 70. 59.45 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE303 HA INTERNATIONAL LLC (0448011215) 280600.63 4610565.60 592.3 32.0 70. 8492.57 0.1 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE304 Stoneco Plant # 110 (0448030014) 277419.55 4605847.70 636.6 70.0 200. 60.76 6.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE305 The Andersons, Inc. (0448031076) 277764.15 4605250.22 634.1 140.0 70. 40.60 3.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE306 The Andersons, Inc. (0448031076) 277764.15 4605250.22 634.1 24.0 70. 23.89 4.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE307 Bulk Molding Compounds, Inc. (0387040001) 279353.55 4603134.11 633.4 55.0 80. 10.88 3.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE308 Bulk Molding Compounds, Inc. (0387040001) 279353.55 4603134.11 633.4 55.0 80. 10.88 3.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE309 Bulk Molding Compounds, Inc. (0387040001) 279353.55 4603134.11 633.4 55.0 80. 10.88 3.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE310 Bulk Molding Compounds, Inc. (0387040001) 279353.55 4603134.11 633.4 55.0 80. 10.88 3.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE311 Graymont Dolime (OH), Inc. (0362000079) 303860.85 4597980.26 621.1 150.0 77. 41.48 5.0 33.330 33.330 33.330 33.330 34.275 34.275 51.513 Yes Yes Yes YesOFFSITE312 Graymont Dolime (OH), Inc. (0362000079) 303860.85 4597980.26 621.1 150.0 77. 41.48 5.0 33.330 33.330 33.330 33.330 33.997 33.997 51.091 Yes Yes Yes YesOFFSITE313 Graymont Dolime (OH), Inc. (0362000079) 303860.85 4597980.26 621.1 150.0 77. 41.48 5.0 33.330 33.330 33.330 33.330 35.313 35.313 53.068 Yes Yes Yes YesOFFSITE314 Graymont Dolime (OH), Inc. (0362000079) 303860.85 4597980.26 621.1 91.0 80. 31.85 1.0 3.293 3.293 3.293 3.293 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE315 Graymont Dolime (OH), Inc. (0362000079) 303860.85 4597980.26 621.1 38.0 80. 58.98 0.6 3.293 3.293 3.293 3.293 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE316 Graymont Dolime (OH), Inc. (0362000079) 303860.85 4597980.26 621.1 38.0 80. 58.98 0.6 3.293 3.293 3.293 3.293 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE317 Graymont Dolime (OH), Inc. (0362000079) 303860.85 4597980.26 621.1 67.5 180. 16.89 2.7 10.180 10.180 10.180 10.180 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE318 Graymont Dolime (OH), Inc. (0362000079) 303860.85 4597980.26 621.1 91.0 180. 51.60 1.2 10.180 10.180 10.180 10.180 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE319 Graymont Dolime (OH), Inc. (0362000079) 303860.85 4597980.26 621.1 40.1 100. 18.34 2.5 0.322 0.322 0.402 0.402 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE320 Graymont Dolime (OH), Inc. (0362000079) 303860.85 4597980.26 621.1 40.1 100. 18.34 2.5 0.306 0.306 0.382 0.382 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE321 Graymont Dolime (OH), Inc. (0362000079) 303860.85 4597980.26 621.1 41.0 80. 43.87 1.1 7.490 7.490 7.490 7.490 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE322 Graymont Dolime (OH), Inc. (0362000079) 303860.85 4597980.26 621.1 58.0 50. 36.86 1.2 0.214 0.214 0.266 0.266 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE323 Troy Energy, LLC (0387000377) 294515.42 4594616.84 643.8 114.5 1100. 150.72 18.0 0.000 0.000 0.000 0.000 58.090 58.090 28.260 No No Yes YesOFFSITE324 Troy Energy, LLC (0387000377) 294515.42 4594616.84 643.8 114.5 1100. 150.72 18.0 0.000 0.000 0.000 0.000 58.090 58.090 28.260 No No Yes YesOFFSITE325 Troy Energy, LLC (0387000377) 294515.42 4594616.84 643.8 114.5 1100. 150.72 18.0 0.000 0.000 0.000 0.000 58.090 58.090 28.260 No No Yes YesOFFSITE326 Troy Energy, LLC (0387000377) 294515.42 4594616.84 643.8 114.5 1100. 150.72 18.0 0.000 0.000 0.000 0.000 58.090 58.090 28.260 No No Yes YesOFFSITE327 Troy Energy, LLC (0387000377) 294515.42 4594616.84 643.8 35.0 882. 125.04 2.0 0.000 0.000 0.000 0.000 4.432 4.432 23.150 No No Yes YesOFFSITE328 Troy Energy, LLC (0387000377) 294515.42 4594616.84 643.8 35.0 882. 125.04 2.0 0.000 0.000 0.000 0.000 4.432 4.432 23.150 No No Yes YesOFFSITE329 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 131.3 287. 55.26 4.2 16.756 16.756 16.756 16.756 15.799 15.799 0.000 Yes Yes Yes NoOFFSITE330 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 131.3 287. 55.26 4.2 17.514 17.514 17.514 17.514 16.584 16.584 0.000 Yes Yes Yes NoOFFSITE331 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 68.6 50. 39.79 4.9 17.514 17.514 17.514 17.514 16.584 16.584 0.000 Yes Yes Yes NoOFFSITE332 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 68.6 50. 39.79 4.9 17.514 17.514 17.514 17.514 16.584 16.584 0.000 Yes Yes Yes NoOFFSITE333 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 68.6 50. 39.79 4.9 17.514 17.514 17.514 17.514 16.584 16.584 0.000 Yes Yes Yes NoOFFSITE334 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 68.6 50. 39.79 4.9 17.514 17.514 17.514 17.514 16.584 16.584 0.000 Yes Yes Yes NoOFFSITE335 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 31.2 50. 39.79 4.9 17.514 17.514 17.514 17.514 16.584 16.584 0.000 Yes Yes Yes NoOFFSITE336 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 22.0 60. 24.81 3.7 0.435 0.435 0.880 0.880 2.696 2.696 0.000 Yes Yes Yes NoOFFSITE337 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 104.0 340. 42.64 3.8 0.435 0.435 0.880 0.880 2.696 2.696 0.000 Yes Yes Yes NoOFFSITE338 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 38.0 80. 27.40 1.7 0.822 0.822 0.822 0.822 0.025 0.025 0.000 Yes Yes Yes NoOFFSITE339 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 44.0 180. 55.73 2.0 3.123 3.123 3.123 3.123 0.066 0.066 0.000 Yes Yes Yes NoOFFSITE340 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 49.0 86. 43.62 1.7 1.014 1.014 1.014 1.014 0.124 0.124 0.000 Yes Yes Yes NoOFFSITE341 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 49.0 86. 43.62 1.7 1.151 1.151 1.151 1.151 0.124 0.124 0.000 Yes Yes Yes NoOFFSITE342 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 49.0 86. 43.62 1.7 0.877 0.877 0.877 0.877 0.124 0.124 0.000 Yes Yes Yes NoOFFSITE343 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 49.0 86. 43.62 1.7 1.151 1.151 1.151 1.151 0.124 0.124 0.000 Yes Yes Yes NoOFFSITE344 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 44.0 180. 55.73 2.0 3.123 3.123 3.123 3.123 0.086 0.086 0.000 Yes Yes Yes NoOFFSITE345 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 44.0 180. 55.73 2.0 3.123 3.123 3.123 3.123 0.078 0.078 0.000 Yes Yes Yes No

Page 290: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Point Source Model Input Data (Sources within 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID

Stack Release

Type

FLAT (Non-

Default) Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Stack Height

(ft)Temperature

(°F)

Exit Velocity (ft/sec)

Stack Diameter

(ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE346 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 124.0 50. 53.08 0.8 0.577 0.577 0.577 0.577 0.000 0.000 0.000 Yes Yes Yes NoOFFSITE347 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 124.0 50. 53.08 0.8 0.577 0.577 0.577 0.577 0.000 0.000 0.000 Yes Yes Yes NoOFFSITE348 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 124.0 50. 53.08 0.8 0.577 0.577 0.577 0.577 0.000 0.000 0.000 Yes Yes Yes NoOFFSITE349 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 124.0 50. 82.94 0.8 0.577 0.577 0.577 0.577 0.000 0.000 0.000 Yes Yes Yes NoOFFSITE350 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 124.0 50. 82.94 0.8 0.577 0.577 0.577 0.577 0.000 0.000 0.000 Yes Yes Yes NoOFFSITE351 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 78.6 50. 44.90 5.1 16.756 16.756 16.756 16.756 15.799 15.799 0.000 Yes Yes Yes NoOFFSITE352 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 78.6 50. 44.90 5.1 16.756 16.756 16.756 16.756 15.799 15.799 0.000 Yes Yes Yes NoOFFSITE353 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 78.6 50. 44.90 5.1 16.756 16.756 16.756 16.756 15.799 15.799 0.000 Yes Yes Yes NoOFFSITE354 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 78.6 50. 44.90 5.1 16.756 16.756 16.756 16.756 15.799 15.799 0.000 Yes Yes Yes NoOFFSITE355 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 78.6 50. 44.90 5.1 16.756 16.756 16.756 16.756 15.799 15.799 0.000 Yes Yes Yes NoOFFSITE356 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 51.0 350. 122.08 2.0 8.180 8.180 8.706 8.706 62.865 62.865 30.419 Yes Yes Yes YesOFFSITE357 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 51.0 350. 122.08 2.0 7.476 7.476 7.956 7.956 57.448 57.448 27.797 Yes Yes Yes YesOFFSITE358 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 51.0 350. 122.08 2.0 8.667 8.667 9.221 9.221 66.586 66.586 32.219 Yes Yes Yes YesOFFSITE359 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 92.0 650. 57.63 5.2 16.469 16.469 19.830 19.830 132.905 132.905 12.421 Yes Yes Yes YesOFFSITE360 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 95.0 350. 51.19 7.2 4.175 4.175 4.710 4.710 142.943 142.943 15.239 Yes Yes Yes YesOFFSITE361 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 37.0 350. 52.42 1.8 8.140 8.140 8.140 8.140 0.788 0.788 0.662 Yes Yes Yes YesOFFSITE362 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 51.0 350. 12.21 2.0 8.630 8.630 8.630 8.630 153.751 153.751 75.000 Yes Yes Yes YesOFFSITE363 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 54.9 60. 87.73 2.2 0.010 0.010 0.028 0.028 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE364 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 58.3 275. 15.92 0.6 0.059 0.059 0.140 0.140 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE365 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 58.3 275. 15.92 0.6 0.059 0.059 0.140 0.140 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE366 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 119.0 60. 108.32 1.4 0.388 0.388 0.961 0.961 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE367 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 119.0 60. 108.32 1.4 1.500 1.500 1.500 1.500 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE368 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 149.0 60. 52.42 0.9 1.500 1.500 1.500 1.500 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE369 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 119.0 60. 28.09 2.3 1.500 1.500 1.500 1.500 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE370 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 119.0 60. 58.05 1.6 1.500 1.500 1.500 1.500 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE371 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 119.0 60. 48.14 2.1 1.500 1.500 1.500 1.500 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE372 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 46.0 60. 29.39 1.7 1.500 1.500 1.500 1.500 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE373 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 20.0 60. 29.39 1.7 1.500 1.500 1.500 1.500 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE374 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 31.2 60. 278.66 0.8 0.128 0.128 0.268 0.268 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE375 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 66.0 60. 131.63 0.5 6.160 6.160 6.160 6.160 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE376 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 47.0 60. 87.73 2.2 6.160 6.160 6.160 6.160 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE377 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 25.0 350. 58.81 1.9 0.168 0.168 0.261 0.261 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE378 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 51.0 350. 12.21 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE379 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. 302362.9 4593267.7 633.3 58.3 275. 64.69 1.9 0.072 0.072 0.255 0.255 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE380 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 36.7 70. 72.98 0.8 0.000 0.000 0.000 0.000 0.000 0.000 1.800 No No No YesOFFSITE381 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 31.3 84. 16.34 5.7 0.000 0.000 0.000 0.000 0.000 0.000 1.800 No No No YesOFFSITE382 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 47.3 77. 36.11 4.2 0.000 0.000 0.000 0.000 0.000 0.000 1.800 No No No YesOFFSITE383 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 47.4 77. 36.11 4.2 0.000 0.000 0.000 0.000 0.000 0.000 1.800 No No No YesOFFSITE384 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 45.5 80. 36.11 4.2 0.000 0.000 0.000 0.000 0.000 0.000 1.800 No No No YesOFFSITE385 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 78. 33.97 5.0 0.000 0.000 0.000 0.000 0.000 0.000 2.128 No No No YesOFFSITE386 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 78. 18.95 5.7 0.000 0.000 0.000 0.000 0.000 0.000 2.128 No No No YesOFFSITE387 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 78. 18.95 5.7 0.000 0.000 0.000 0.000 0.000 0.000 2.128 No No No YesOFFSITE388 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 78. 33.97 5.0 0.000 0.000 0.000 0.000 0.000 0.000 1.584 No No No YesOFFSITE389 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 78. 18.95 5.7 0.000 0.000 0.000 0.000 0.000 0.000 1.584 No No No YesOFFSITE390 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 78. 18.95 5.7 0.000 0.000 0.000 0.000 0.000 0.000 1.584 No No No YesOFFSITE391 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE392 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE393 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE394 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE395 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE396 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE397 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE398 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE399 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE400 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE401 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE402 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE403 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE404 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE405 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE406 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE407 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE408 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE409 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE410 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE411 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE412 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE413 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE414 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE415 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE416 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE417 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No Yes

Page 291: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Point Source Model Input Data (Sources within 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID

Stack Release

Type

FLAT (Non-

Default) Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Stack Height

(ft)Temperature

(°F)

Exit Velocity (ft/sec)

Stack Diameter

(ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE418 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE419 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE420 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE421 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE422 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE423 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE424 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE425 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE426 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE427 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE428 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE429 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE430 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE431 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE432 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE433 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE434 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE435 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE436 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE437 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE438 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE439 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE440 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE441 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE442 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE443 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE444 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE445 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE446 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE447 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE448 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE449 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE450 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.592 No No No YesOFFSITE451 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE452 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE453 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE454 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE455 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE456 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE457 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE458 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE459 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE460 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE461 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE462 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE463 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE464 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE465 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE466 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.500 No No No YesOFFSITE467 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.500 No No No YesOFFSITE468 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.500 No No No YesOFFSITE469 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.500 No No No YesOFFSITE470 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.500 No No No YesOFFSITE471 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.500 No No No YesOFFSITE472 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.500 No No No YesOFFSITE473 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.500 No No No YesOFFSITE474 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.500 No No No YesOFFSITE475 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.500 No No No YesOFFSITE476 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE477 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE478 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE479 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE480 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE481 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE482 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE483 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE484 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE485 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE486 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE487 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE488 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE489 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No Yes

Page 292: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Point Source Model Input Data (Sources within 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID

Stack Release

Type

FLAT (Non-

Default) Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Stack Height

(ft)Temperature

(°F)

Exit Velocity (ft/sec)

Stack Diameter

(ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE490 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE491 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE492 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE493 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE494 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE495 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.472 No No No YesOFFSITE496 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.708 No No No YesOFFSITE497 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.708 No No No YesOFFSITE498 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.708 No No No YesOFFSITE499 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.708 No No No YesOFFSITE500 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.708 No No No YesOFFSITE501 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.708 No No No YesOFFSITE502 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.708 No No No YesOFFSITE503 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.708 No No No YesOFFSITE504 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.708 No No No YesOFFSITE505 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.708 No No No YesOFFSITE506 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.768 No No No YesOFFSITE507 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.768 No No No YesOFFSITE508 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.768 No No No YesOFFSITE509 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.768 No No No YesOFFSITE510 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.768 No No No YesOFFSITE511 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.768 No No No YesOFFSITE512 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.768 No No No YesOFFSITE513 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.768 No No No YesOFFSITE514 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.768 No No No YesOFFSITE515 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.768 No No No YesOFFSITE516 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.813 No No No YesOFFSITE517 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.813 No No No YesOFFSITE518 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.813 No No No YesOFFSITE519 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.813 No No No YesOFFSITE520 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.813 No No No YesOFFSITE521 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.813 No No No YesOFFSITE522 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.813 No No No YesOFFSITE523 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.813 No No No YesOFFSITE524 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.813 No No No YesOFFSITE525 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.813 No No No YesOFFSITE526 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.830 No No No YesOFFSITE527 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.830 No No No YesOFFSITE528 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.830 No No No YesOFFSITE529 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.830 No No No YesOFFSITE530 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.830 No No No YesOFFSITE531 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.830 No No No YesOFFSITE532 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.830 No No No YesOFFSITE533 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.830 No No No YesOFFSITE534 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.830 No No No YesOFFSITE535 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.830 No No No YesOFFSITE536 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE537 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE538 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE539 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE540 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE541 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE542 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE543 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE544 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE545 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE546 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE547 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE548 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE549 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE550 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE551 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE552 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE553 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE554 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE555 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.857 No No No YesOFFSITE556 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.240 No No No YesOFFSITE557 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.240 No No No YesOFFSITE558 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.240 No No No YesOFFSITE559 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.240 No No No YesOFFSITE560 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.240 No No No YesOFFSITE561 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.240 No No No Yes

Page 293: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Point Source Model Input Data (Sources within 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID

Stack Release

Type

FLAT (Non-

Default) Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Stack Height

(ft)Temperature

(°F)

Exit Velocity (ft/sec)

Stack Diameter

(ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE562 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.240 No No No YesOFFSITE563 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.240 No No No YesOFFSITE564 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.240 No No No YesOFFSITE565 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.240 No No No YesOFFSITE566 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.240 No No No YesOFFSITE567 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.240 No No No YesOFFSITE568 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.240 No No No YesOFFSITE569 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.240 No No No YesOFFSITE570 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.240 No No No YesOFFSITE571 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.379 No No No YesOFFSITE572 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.379 No No No YesOFFSITE573 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.379 No No No YesOFFSITE574 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.379 No No No YesOFFSITE575 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.379 No No No YesOFFSITE576 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.379 No No No YesOFFSITE577 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.379 No No No YesOFFSITE578 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.379 No No No YesOFFSITE579 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.379 No No No YesOFFSITE580 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.379 No No No YesOFFSITE581 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.379 No No No YesOFFSITE582 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.379 No No No YesOFFSITE583 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.379 No No No YesOFFSITE584 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.379 No No No YesOFFSITE585 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.379 No No No YesOFFSITE586 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE587 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE588 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE589 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE590 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE591 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE592 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE593 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE594 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE595 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE596 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE597 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE598 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE599 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE600 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE601 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE602 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE603 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE604 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE605 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.672 No No No YesOFFSITE606 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.188 No No No YesOFFSITE607 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.188 No No No YesOFFSITE608 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.188 No No No YesOFFSITE609 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.188 No No No YesOFFSITE610 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.188 No No No YesOFFSITE611 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.153 No No No YesOFFSITE612 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.153 No No No YesOFFSITE613 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.153 No No No YesOFFSITE614 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.153 No No No YesOFFSITE615 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 20.0 300. 632.31 1.9 0.000 0.000 0.000 0.000 0.000 0.000 0.153 No No No YesOFFSITE616 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE617 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE618 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE619 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE620 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE621 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE622 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE623 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE624 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE625 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE626 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE627 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE628 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE629 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE630 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE631 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE632 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE633 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No Yes

Page 294: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Point Source Model Input Data (Sources within 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID

Stack Release

Type

FLAT (Non-

Default) Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Stack Height

(ft)Temperature

(°F)

Exit Velocity (ft/sec)

Stack Diameter

(ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE634 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE635 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE636 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE637 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE638 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE639 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE640 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE641 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE642 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE643 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE644 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE645 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE646 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE647 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE648 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE649 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE650 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE651 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE652 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE653 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE654 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE655 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE656 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE657 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE658 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE659 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE660 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE661 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE662 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE663 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE664 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE665 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE666 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE667 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE668 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE669 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE670 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE671 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE672 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE673 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE674 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE675 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE676 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE677 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE678 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE679 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE680 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE681 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE682 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE683 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE684 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE685 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE686 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE687 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE688 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE689 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE690 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE691 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE692 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE693 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE694 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE695 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE696 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE697 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE698 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE699 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE700 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE701 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE702 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE703 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE704 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE705 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No Yes

Page 295: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Point Source Model Input Data (Sources within 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID

Stack Release

Type

FLAT (Non-

Default) Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Stack Height

(ft)Temperature

(°F)

Exit Velocity (ft/sec)

Stack Diameter

(ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE706 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE707 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE708 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE709 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE710 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE711 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE712 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE713 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE714 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 130. 22.87 5.7 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE715 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE716 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE717 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE718 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE719 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE720 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 80.0 300. 17.33 7.0 0.000 0.000 0.000 0.000 0.000 0.000 6.240 No No No YesOFFSITE721 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 78. 33.97 5.0 0.000 0.000 0.000 0.000 0.000 0.000 18.200 No No No YesOFFSITE722 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 78. 18.95 5.7 0.000 0.000 0.000 0.000 0.000 0.000 18.200 No No No YesOFFSITE723 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 78. 18.95 5.7 0.000 0.000 0.000 0.000 0.000 0.000 18.200 No No No YesOFFSITE724 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 78. 33.97 5.0 0.000 0.000 0.000 0.000 0.000 0.000 18.200 No No No YesOFFSITE725 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 78. 18.95 5.7 0.000 0.000 0.000 0.000 0.000 0.000 18.200 No No No YesOFFSITE726 Johns Manville - Waterville 07 (0448000013) 272988.87 4600614.48 638.2 62.0 78. 18.95 5.7 0.000 0.000 0.000 0.000 0.000 0.000 18.200 No No No YesOFFSITE727 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 51.6 70. 18.86 2.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE728 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 51.6 70. 18.86 2.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE729 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 51.6 70. 18.86 2.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE730 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 51.6 70. 18.86 2.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE731 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 51.6 70. 18.86 2.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE732 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 51.6 70. 13.59 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE733 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 53.7 70. 21.93 2.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE734 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 53.7 70. 21.93 2.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE735 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 55.9 70. 10.19 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE736 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 55.9 300. 16.99 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE737 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 55.9 300. 62.81 1.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE738 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 50.0 1600. 52.86 4.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE739 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 55.9 300. 12.23 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE740 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 53.7 70. 21.93 2.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE741 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 50.0 1600. 52.86 4.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE742 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 50.0 1600. 52.86 4.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE743 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 51.3 70. 41.14 4.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE744 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 61.8 70. 10.03 2.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE745 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 51.3 70. 41.14 4.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE746 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 61.8 70. 10.03 2.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE747 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 51.3 70. 41.14 4.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE748 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 61.8 70. 10.03 2.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE749 Kokosing Materials - Plant 521 (0372002004) 303873.49 4590756.5 633.1 1.0 30. 0.21 0.1 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE750 Materion Brush Inc. (0362000009) 314987.71 4595346.37 596.8 27.0 450. 25.13 1.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE751 Materion Brush Inc. (0362000009) 314987.71 4595346.37 596.8 27.0 450. 25.13 1.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE752 Materion Brush Inc. (0362000009) 314987.71 4595346.37 596.8 36.0 450. 6.16 1.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE753 Materion Brush Inc. (0362000009) 314987.71 4595346.37 596.8 40.0 450. 8.17 1.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE754 Materion Brush Inc. (0362000009) 314987.71 4595346.37 596.8 40.0 450. 8.17 1.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE755 Materion Brush Inc. (0362000009) 314987.71 4595346.37 596.8 175.0 115. 16.59 8.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE756 Materion Brush Inc. (0362000009) 314987.71 4595346.37 596.8 299.0 100. 32.08 9.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE757 Materion Brush Inc. (0362000009) 314987.71 4595346.37 596.8 299.0 100. 32.08 9.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE758 Materion Brush Inc. (0362000009) 314987.71 4595346.37 596.8 175.0 115. 16.59 8.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE759 Materion Brush Inc. (0362000009) 314987.71 4595346.37 596.8 43.0 96. 72.98 4.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE760 Materion Brush Inc. (0362000009) 314987.71 4595346.37 596.8 43.7 207. 40.76 0.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE761 Materion Brush Inc. (0362000009) 314987.71 4595346.37 596.8 43.7 186. 59.45 0.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE762 Materion Brush Inc. (0362000009) 314987.71 4595346.37 596.8 40.0 50. 47.18 1.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE763 Materion Brush Inc. (0362000009) 314987.71 4595346.37 596.8 50.3 50. 37.15 4.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE764 Materion Brush Inc. (0362000009) 314987.71 4595346.37 596.8 299.0 100. 32.08 9.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE765 Bowling Green State Univ (0387029240) 277137.92 4588445.23 672.6 65.0 190. 117.63 3.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE766 Bowling Green State Univ (0387029240) 277137.92 4588445.23 672.6 65.0 190. 117.63 3.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE767 Bowling Green State Univ (0387029240) 277137.92 4588445.23 672.6 65.0 190. 117.63 3.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE768 Ottawa County Landfill Gas Power Station (03620 330311.32 4598234.71 576.1 32.8 869. 170.59 1.1 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE769 Port Clinton Landfill (0362010118) 331019.44 4598773.52 576.1 30.0 1000. 34.10 0.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE770 Carmeuse Lime Inc Millersville Operations (03720 308908.24 4577351.19 682.0 10.0 150. 1273.89 1.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE771 Carmeuse Lime Inc Millersville Operations (03720 308908.24 4577351.19 682.0 10.0 150. 1295.12 1.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE772 Carmeuse Lime Inc Millersville Operations (03720 308908.24 4577351.19 682.0 1.0 77. 1133.76 1.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE773 Carmeuse Lime Inc Millersville Operations (03720 308908.24 4577351.19 682.0 58.3 77. 0.03 2.9 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE774 AMP Fremont Energy Center (0372030241) 318916.45 4582958.22 622.8 64.8 650. 62.27 11.4 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE775 AMP Fremont Energy Center (0372030241) 318916.45 4582958.22 622.8 64.8 650. 62.27 11.4 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE776 AMP Fremont Energy Center (0372030241) 318916.45 4582958.22 622.8 41.9 85. 24.09 13.1 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE777 ABC Inoac Exterior Systems, LLC (0372030199) 320083.85 4581478.23 626.6 29.0 176. 20.73 1.6 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No No

Page 296: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Point Source Model Input Data (Sources within 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID

Stack Release

Type

FLAT (Non-

Default) Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Stack Height

(ft)Temperature

(°F)

Exit Velocity (ft/sec)

Stack Diameter

(ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE778 ABC Inoac Exterior Systems, LLC (0372030199) 320083.85 4581478.23 626.6 44.0 361. 37.18 1.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE779 ABC Inoac Exterior Systems, LLC (0372030199) 320083.85 4581478.23 626.6 40.0 175. 27.56 2.2 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE780 ABC Inoac Exterior Systems, LLC (0372030199) 320083.85 4581478.23 626.6 44.0 70. 45.95 3.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE781 ABC Inoac Exterior Systems, LLC (0372030199) 320083.85 4581478.23 626.6 29.0 70. 45.95 3.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE782 ABC Inoac Exterior Systems, LLC (0372030199) 320083.85 4581478.23 626.6 44.0 70. 36.80 1.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE783 ABC Inoac Exterior Systems, LLC (0372030199) 320083.85 4581478.23 626.6 29.0 70. 2.35 3.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE784 ABC Inoac Exterior Systems, LLC (0372030199) 320083.85 4581478.23 626.6 29.0 70. 45.95 3.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE785 ABC Inoac Exterior Systems, LLC (0372030199) 320083.85 4581478.23 626.6 44.0 70. 45.95 3.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE786 ABC Inoac Exterior Systems, LLC (0372030199) 320083.85 4581478.23 626.6 44.0 70. 36.80 1.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE787 ABC Inoac Exterior Systems, LLC (0372030199) 320083.85 4581478.23 626.6 44.0 70. 45.95 3.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE788 ABC Inoac Exterior Systems, LLC (0372030199) 320083.85 4581478.23 626.6 44.0 70. 45.95 3.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE789 P.H. Glatfelter Co. - Fremont Facility (0372030100 320387.34 4581532.92 625.2 36.7 430. 21.77 1.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE790 P.H. Glatfelter Co. - Fremont Facility (0372030100 320387.34 4581532.92 625.2 30.0 250. 12.67 3.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE791 P.H. Glatfelter Co. - Fremont Facility (0372030100 320387.34 4581532.92 625.2 30.0 250. 12.67 3.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE792 P.H. Glatfelter Co. - Fremont Facility (0372030100 320387.34 4581532.92 625.2 30.0 250. 12.67 3.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE793 P.H. Glatfelter Co. - Fremont Facility (0372030100 320387.34 4581532.92 625.2 17.5 102. 18.22 1.4 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE794 P.H. Glatfelter Co. - Fremont Facility (0372030100 320387.34 4581532.92 625.2 30.0 68. 86.25 0.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE795 Style Crest Enterprises, Inc. (0372030210) 323218.14 4582265.41 615.6 36.8 90. 72.98 1.6 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE796 Style Crest Enterprises, Inc. (0372030210) 323218.14 4582265.41 615.6 36.8 90. 72.98 1.6 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE797 Style Crest Enterprises, Inc. (0372030210) 323218.14 4582265.41 615.6 34.3 90. 93.42 1.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE798 WORTHINGTON STEEL (0326000076) 247120.16 4607312.75 732.9 49.0 400. 8.15 3.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE799 WORTHINGTON STEEL (0326000076) 247120.16 4607312.75 732.9 49.0 400. 8.15 3.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE800 WORTHINGTON STEEL (0326000076) 247120.16 4607312.75 732.9 155.0 600. 50.53 5.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE801 WORTHINGTON STEEL (0326000076) 247120.16 4607312.75 732.9 91.0 100. 44.08 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE802 WORTHINGTON STEEL (0326000076) 247120.16 4607312.75 732.9 78.9 400. 13.71 4.4 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE803 WORTHINGTON STEEL (0326000076) 247120.16 4607312.75 732.9 155.0 600. 50.53 5.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE804 WORTHINGTON STEEL (0326000076) 247120.16 4607312.75 732.9 70.0 126. 16.51 3.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE805 The Kraft Heinz Company (0372030070) 324902.61 4580773.66 617.9 60.0 400. 42.47 4.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE806 Charter Steel (0387000376) 297129.65 4568812.83 717.1 36.5 593. 39.66 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE807 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 13.40 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE808 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 27.15 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE809 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 13.40 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE810 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 13.40 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE811 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 27.15 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE812 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 13.40 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE813 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 13.40 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE814 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 27.15 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE815 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 13.40 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE816 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 13.40 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE817 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 27.15 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE818 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 13.40 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE819 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 13.40 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE820 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 27.15 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE821 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 13.40 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE822 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 13.40 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE823 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 27.15 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE824 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 13.40 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE825 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 13.40 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE826 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 27.15 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE827 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 13.40 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE828 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 13.40 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE829 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 27.15 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE830 Charter Steel (0387000376) 297129.65 4568812.83 717.1 45.0 350. 13.40 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE831 Charter Steel (0387000376) 297129.65 4568812.83 717.1 25.7 70. 50.17 2.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE832 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 75.0 300. 5.31 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE833 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 75.0 300. 5.31 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE834 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 28.0 300. 5.31 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE835 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 28.0 300. 5.31 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE836 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 450. 33.06 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE837 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 80. 32.93 3.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE838 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 400. 33.06 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE839 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 400. 33.06 1.7 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE840 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 80. 23.89 4.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE841 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 500. 13.27 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE842 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 200. 14.95 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE843 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 80. 18.84 1.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE844 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 350. 11.21 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE845 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 400. 11.21 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE846 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 400. 11.21 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE847 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 250. 11.21 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE848 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 500. 13.27 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE849 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 200. 14.95 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No No

Page 297: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Point Source Model Input Data (Sources within 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID

Stack Release

Type

FLAT (Non-

Default) Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Stack Height

(ft)Temperature

(°F)

Exit Velocity (ft/sec)

Stack Diameter

(ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE850 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 80. 18.84 1.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE851 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 350. 11.21 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE852 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 400. 11.21 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE853 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 400. 11.21 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE854 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 250. 11.21 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE855 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 500. 13.27 2.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE856 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 200. 14.95 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE857 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 400. 14.15 3.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE858 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 400. 11.21 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE859 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 250. 13.59 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE860 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 80. 18.34 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE861 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 80. 23.40 3.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE862 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 80. 18.34 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE863 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 80. 23.40 3.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE864 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 80. 18.34 2.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE865 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 65.0 80. 23.40 3.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE866 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 111.5 1218. 15.52 5.6 0.000 0.000 0.000 0.000 22.600 22.600 7.910 No No Yes YesOFFSITE867 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 111.5 1253. 7.63 5.6 0.000 0.000 0.000 0.000 22.600 22.600 7.910 No No Yes YesOFFSITE868 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 111.5 380. 5.62 5.6 0.000 0.000 0.000 0.000 9.000 9.000 4.200 No No Yes YesOFFSITE869 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 70.0 200. 0.01 20.1 0.000 0.000 0.000 0.000 2.000 2.000 0.400 No No Yes YesOFFSITE870 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 70.0 200. 0.01 20.1 0.000 0.000 0.000 0.000 2.000 2.000 0.400 No No Yes YesOFFSITE871 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 70.0 200. 0.01 20.1 0.000 0.000 0.000 0.000 1.600 1.600 0.320 No No Yes YesOFFSITE872 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 70.0 200. 0.01 20.1 0.000 0.000 0.000 0.000 1.600 1.600 0.320 No No Yes YesOFFSITE873 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 70.0 200. 0.01 20.1 0.000 0.000 0.000 0.000 1.600 1.600 0.320 No No Yes YesOFFSITE874 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 70.0 200. 0.01 20.1 0.000 0.000 0.000 0.000 2.000 2.000 0.400 No No Yes YesOFFSITE875 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 91.5 150. 753.78 6.5 0.000 0.000 0.000 0.000 179.600 179.600 2362.500 No No Yes YesOFFSITE876 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 91.5 230. 766.34 6.5 0.000 0.000 0.000 0.000 179.600 179.600 2362.500 No No Yes YesOFFSITE877 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 70.0 200. 0.01 20.1 0.000 0.000 0.000 0.000 179.600 179.600 2362.500 No No Yes YesOFFSITE878 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 91.5 150. 753.78 6.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE879 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 91.5 230. 766.34 6.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE880 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 70.0 200. 0.01 20.1 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE881 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 91.5 150. 753.78 6.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE882 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 91.5 230. 766.34 6.5 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE883 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 70.0 200. 0.01 20.1 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE884 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 39.5 50. 24.88 0.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE885 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 39.5 50. 24.88 0.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE886 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 39.5 50. 24.88 0.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE887 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 39.5 50. 24.88 0.8 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE888 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 70.0 100. 0.00 23.3 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE889 VIENNA JUNCTION LANDFILL 291000.00 4625000.00 584.8 50.0 1400 0.99 8.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE890 BROWNING-FERRIS INDUSTRIES 291000.00 4625000.00 584.8 40 1400 73.14 10.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE891 R J MARSHALL COMPANY 291780.00 4628840.00 591.2 20 70 1.00 0.83 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE892 R J MARSHALL COMPANY 291780.00 4628840.00 591.2 50 70 1.00 1.08 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE893 J.R. WHITING CO 296440.00 4629490.00 580.0 23 70 3.31 0.80 0.000 0.000 0.821 0.821 0.000 0.000 0.000 No Yes Yes YesOFFSITE894 J.R. WHITING CO 296440.00 4629490.00 580.0 52 70 79.94 2.50 0.000 0.000 0.821 0.821 0.000 0.000 0.000 No Yes Yes YesOFFSITE895 J.R. WHITING CO 296440.00 4629490.00 580.0 18 70 113.52 4.83 0.000 0.000 0.821 0.821 0.000 0.000 0.000 No Yes Yes YesOFFSITE896 J.R. WHITING CO 296440.00 4629490.00 580.0 15 70 55.25 3.50 0.000 0.000 0.821 0.821 0.000 0.000 0.000 No Yes Yes YesOFFSITE897 J.R. WHITING CO 296440.00 4629490.00 580.0 7 70 8.49 0.50 0.000 0.000 2.595 2.595 0.000 0.000 0.000 No Yes Yes YesOFFSITE898 J.R. WHITING CO 296440.00 4629490.00 580.0 115 70 0.42 2.25 0.000 0.000 1.297 1.297 0.000 0.000 0.000 No Yes Yes YesOFFSITE899 J.R. WHITING CO 296440.00 4629490.00 580.0 8 70 3.31 0.80 0.000 0.000 1.297 1.297 0.000 0.000 0.000 No Yes Yes YesOFFSITE900 J.R. WHITING CO 296440.00 4629490.00 580.0 297 285 64.70 11.00 0.000 0.000 25.512 25.512 187.623 187.623 20.076 No Yes Yes YesOFFSITE901 J.R. WHITING CO 296440.00 4629490.00 580.0 297 288 64.70 11.00 0.000 0.000 78.218 78.218 182.881 182.881 21.481 No Yes Yes YesOFFSITE902 J.R. WHITING CO 296440.00 4629490.00 580.0 297 286 70.26 11.90 0.000 0.000 117.822 117.822 216.370 216.370 26.763 No Yes Yes YesOFFSITE903 CONSUMERS ENERGY COMPANY 296440.00 4629490.00 580.0 297 330 44.92 11.00 0.000 0.000 840.000 840.000 0.000 0.000 91.324 No Yes Yes YesOFFSITE904 CONSUMERS ENERGY COMPANY 296440.00 4629490.00 580.0 18 70 1.00 4.83 0.000 0.000 8.484 8.484 0.000 0.000 0.000 No Yes Yes YesOFFSITE905 STONECO, INC 278652.00 4625040.00 679.2 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE906 GERKEN MATERIALS, INC 278300.00 4625040.00 626.5 44 1.00 2.50 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE907 STONECO, INC 298000.00 4640600.00 602.2 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE908 GERKEN MATERIALS INC 298000.00 4640600.00 602.2 30 300 85.59 3.80 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE909 COUNTRYMARK COOPERATIVE, INC 270766.00 4627257.00 691.6 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE910 Gerdau MacSteel Monroe 304524.00 4640317.00 576.4 41.3 70 6.77 2.63 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No YesOFFSITE911 Gerdau MacSteel Monroe 304524.00 4640317.00 576.4 40 70 225.87 0.97 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No YesOFFSITE912 Gerdau MacSteel Monroe 304524.00 4640317.00 576.4 136 143 84.17 1.67 0.000 0.000 0.000 0.000 0.000 0.000 41.417 No No No YesOFFSITE913 Gerdau MacSteel Monroe 304524.00 4640317.00 576.4 120 115 82.32 11.30 0.000 0.000 0.000 0.000 0.000 0.000 113.443 No No No YesOFFSITE914 Gerdau MacSteel Monroe 304524.00 4640317.00 576.4 145 950 25.41 9.00 0.000 0.000 0.000 0.000 0.000 0.000 5.659 No No No YesOFFSITE915 Gerdau MacSteel Monroe 304524.00 4640317.00 576.4 80 480 29.19 3.33 0.000 0.000 0.000 0.000 0.000 0.000 3.728 No No No YesOFFSITE916 GERDAU MACSTEEL MONROE 304524.00 4640317.00 576.4 185 70.0 50.00 8.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No YesOFFSITE917 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 581.5 34 850 135.78 0.50 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE918 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 581.5 34 850 135.78 0.50 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE919 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 581.5 34 850 135.78 0.50 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE920 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 581.5 34 850 135.78 0.50 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE921 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 581.5 579 120 58.18 28.00 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes Yes

Page 298: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Point Source Model Input Data (Sources within 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID

Stack Release

Type

FLAT (Non-

Default) Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Stack Height

(ft)Temperature

(°F)

Exit Velocity (ft/sec)

Stack Diameter

(ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE922 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 581.5 700 270 127.99 28.00 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE923 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 581.5 115 777 164.99 1.00 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE924 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 581.5 579 120 58.18 28.00 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE925 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 581.5 579 120 58.18 28.00 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE926 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 581.5 579 120 58.18 28.00 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE927 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 581.5 20 750 7.46 2.67 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE928 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 581.5 20 750 7.46 2.67 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE929 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 581.5 20 750 7.46 2.67 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE930 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 581.5 20 750 7.46 2.67 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE931 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 581.5 20 750 7.46 2.67 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE932 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 581.5 231 900 1.42 9.00 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE933 DTE ELECTRIC COMPANY 305350.00 4640200.00 581.5 805 70.0 1.00 28.00 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE934 MICHIGAN PAVING & MATERIALS COMPANY 304500.00 4640700.00 582.1 130 550 1.00 2.50 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE935 IKO MONROE, INC 300200.00 4644200.00 598.5 56 480 1.00 4.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE936 IKO MONROE, INC 300200.00 4644200.00 598.5 42 70.0 1.00 2.67 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE937 MID-AMERICAN RECYCLERS, INC 307776.00 4645845.00 585.5 90 280 1.00 4.50 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE938 SPARTAN STEEL COATING 305095.00 4647120.00 592.2 65 95 42.43 2.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE939 SPARTAN STEEL COATING 305095.00 4647120.00 592.2 156 650 37.72 7.50 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE940 SPARTAN STEEL COATING 305095.00 4647120.00 592.2 65 95 1.00 2.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE941 DTE ENERGY 312850.00 4647650.00 580.0 22 958 366.91 0.50 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE942 HOLNAM, INC 279800.00 4652300.00 669.8 350 340 1.00 15.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE943 HOLCIM (US), INC 279800.00 4652300.00 669.8 20 68 1.00 0.83 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE944 GUARDIAN INDUSTRIES 304915.00 4662490.00 614.0 14 70 57.75 1.92 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes NoOFFSITE945 GUARDIAN INDUSTRIES 304915.00 4662490.00 614.0 12 75 2.19 0.73 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes NoOFFSITE946 GUARDIAN INDUSTRIES 304915.00 4662490.00 614.0 9 50 1.00 1.26 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes NoOFFSITE947 GUARDIAN INDUSTRIES 304915.00 4662490.00 614.0 23 70 53.04 2.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes NoOFFSITE948 GUARDIAN INDUSTRIES 304915.00 4662490.00 614.0 26 950 160.29 1.50 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes NoOFFSITE949 GUARDIAN INDUSTRIES 304915.00 4662490.00 614.0 199 955.4 31.00 8.50 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes NoOFFSITE950 GUARDIAN INDUSTRIES 304915.00 4662490.00 614.0 199 724.9 33.24 8.50 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes NoOFFSITE951 MICHIGAN AGRICULTURAL COMMODITIES 263500.00 4634500.00 690.9 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE952 MICHIGAN AGRICULTURAL COMMODITIES 263500.00 4634500.00 690.9 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE953 WACKER CHEMICAL CORP 255600.00 4648000.00 768.5 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE954 WACKER CHEMICAL CORP 255600.00 4648000.00 768.5 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE955 WACKER CHEMICAL CORP 255600.00 4648000.00 768.5 58 450 20.03 1.67 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE956 WACKER CHEMICAL CORP 255600.00 4648000.00 768.5 58 450 20.03 1.67 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE957 WACKER CHEMICAL CORP 255600.00 4648000.00 768.5 58 450 20.03 1.67 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE958 WACKER CHEMICAL CORP 255600.00 4648000.00 768.5 58 450 12.91 2.08 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE959 WACKER CHEMICAL CORP 255600.00 4648000.00 768.5 57 750 5.96 2.50 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE960 ADRIAN LANDFILL 251300.00 4642135.00 807.6 20 77 16.48 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE961 ADRIAN ENERGY ASSOICATES 251300.00 4642135.00 807.6 24 1400 1.00 0.67 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE962 ADRIAN ENERGY ASSOCIATES 251300.00 4642135.00 807.6 25 780 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE963 ADRIAN LANDFILL 251300.00 4642135.00 807.6 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE964 Faurecia Interior Systems Saline, LLC 271557.00 4627931.00 684.0 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE965 Faurecia Interior Systems Saline, LLC 271557.00 4627931.00 684.0 39.6 80 36.70 1.70 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE966 Faurecia Interior Systems Saline, LLC 271557.00 4627931.00 684.0 36.4 180 45.26 1.50 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE967 AUTOMOTIVE COMPONENTS HOLDINGS, LLC 271557.00 4627931.00 684.0 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE968 Georgia-Pacific Corrugated II LLC 278400.00 4663100.00 703.1 38 500 42.43 2.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE969 Georgia-Pacific Corrugated II LLC 278400.00 4663100.00 703.1 28 50 53.04 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE970 Georgia-Pacific Corrugated II LLC 278400.00 4663100.00 703.1 42 75 1.00 0.56 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE971 B.O.P. FEDERAL CORRECTIONAL INSTITUTE 279050.00 4663500.00 699.9 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE972 BOP FED CORRECTIONAL INSTIT 279050.00 4663500.00 699.9 31 301 1.00 2.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE973 GS Materials, LLC 253000.00 4646500.00 708.2 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE974 G S MATERIALS, LLC 253000.00 4646500.00 708.2 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE975 CARLETON FARMS LANDFILL 299500.00 4662700.00 640.2 40.08 100 0.59 10.00 0.000 0.000 0.000 0.000 0.000 0.000 57.735 No No No YesOFFSITE976 CARLETON FARMS LANDFILL 299500.00 4662700.00 640.2 35 1400 27.58 1.00 0.000 0.000 0.000 0.000 0.000 0.000 137.930 No No No YesOFFSITE977 CARLETON FARMS LANDFILL 299500.00 4662700.00 640.2 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 36.260 No No No YesOFFSITE978 CARLETON FARMS LANDFILL 299500.00 4662700.00 640.2 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 48.459 No No No YesOFFSITE979 SUMPTER ENERGY ASSOCIATES 299500.00 4662700.00 640.2 27 780 121.03 1.00 0.000 0.000 0.000 0.000 0.000 0.000 7.280 No No No YesOFFSITE980 CARLETON FARMS LANDFILL 299500.00 4662700.00 640.2 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No YesOFFSITE981 U S SILICA CO 315500.00 4658500.00 587.5 60 180 54.48 3.45 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE982 U S SILICA CO 315500.00 4658500.00 587.5 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE983 U S SILICA CO 315500.00 4658500.00 587.5 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE984 U S SILICA CO 315500.00 4658500.00 587.5 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE985 U S SILICA CO 315500.00 4658500.00 587.5 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE986 U S SILICA CO 315500.00 4658500.00 587.5 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE987 U S SILICA CO 315500.00 4658500.00 587.5 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE988 U S SILICA CO 315500.00 4658500.00 587.5 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE989 U S SILICA CO 315500.00 4658500.00 587.5 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE990 U S SILICA CO 315500.00 4658500.00 587.5 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE991 U S SILICA CO 315500.00 4658500.00 587.5 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE992 U S SILICA CO 315500.00 4658500.00 587.5 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE993 U S SILICA COMPANY 315500.00 4658500.00 587.5 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No No

Page 299: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Point Source Model Input Data (Sources within 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID

Stack Release

Type

FLAT (Non-

Default) Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Stack Height

(ft)Temperature

(°F)

Exit Velocity (ft/sec)

Stack Diameter

(ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE994 U S SILICA COMPANY 315500.00 4658500.00 587.5 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE995 RECKITT BENCKISER, INC 314400.00 4659400.00 577.1 83 85 264.70 1.17 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE996 CITY SAND & LANDFILL INC 293500.00 4664600.00 652.5 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE997 FLAT ROCK METAL INC 310089.00 4663986.00 590.0 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE998 FLAT ROCK METAL INC 310089.00 4663986.00 590.0 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE999 FLAT ROCK METAL INC 310089.00 4663986.00 590.0 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1000 FLAT ROCK METAL INC 310089.00 4663986.00 590.0 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1001 FLAT ROCK METAL INC 310089.00 4663986.00 590.0 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1002 FLAT ROCK METAL INC 310089.00 4663986.00 590.0 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1003 FLAT ROCK METAL INC 310089.00 4663986.00 590.0 5.0 70.0 1.00 1.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1004 FLAT ROCK METAL, INC 310089.00 4663986.00 590.0 35 70 1.00 3.00 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No No

Page 300: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Volume Source Model Input Data (Sources sithin 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Release Height

(ft) Sigma Y (ft) Sigma Z (ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE1005 TOLEDO SHREDDING LLC (0448011575) 293963.00 4616843.00 590.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1006 City of Toledo, Division of Water Reclamation (044 293513.18 4618147.23 576.9 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.042 0.042 0.029 No No Yes YesOFFSITE1007 City of Toledo, Division of Water Reclamation (044 293513.18 4618147.23 576.9 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.041 0.041 0.041 No No Yes YesOFFSITE1008 City of Toledo, Division of Water Reclamation (044 293513.18 4618147.23 576.9 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.017 0.017 0.014 No No Yes YesOFFSITE1009 Mondelez Global LLC - Toledo Flour Mill (04480100 291939.00 4615597.00 597.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes No NoOFFSITE1010 Mondelez Global LLC - Toledo Flour Mill (04480100 291939.00 4615597.00 597.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes No NoOFFSITE1011 Mondelez Global LLC - Toledo Flour Mill (04480100 291939.00 4615597.00 597.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes No NoOFFSITE1012 Mondelez Global LLC - Toledo Flour Mill (04480100 291939.00 4615597.00 597.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes No NoOFFSITE1013 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 5.0 10.0 10.0 0.091 0.091 0.099 0.099 0.000 0.000 0.011 Yes Yes Yes YesOFFSITE1014 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 5.0 10.0 10.0 0.359 0.359 0.393 0.393 0.000 0.000 0.037 Yes Yes Yes YesOFFSITE1015 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 5.0 10.0 10.0 0.019 0.019 0.019 0.019 0.233 0.233 0.025 Yes Yes Yes YesOFFSITE1016 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 5.0 10.0 10.0 0.019 0.019 0.019 0.019 0.233 0.233 0.025 Yes Yes Yes YesOFFSITE1017 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.001 0.001 0.057 Yes Yes Yes YesOFFSITE1018 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 5.0 10.0 10.0 0.000 0.000 1.047 1.047 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1019 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 15.0 10.0 10.0 0.000 0.000 0.826 0.826 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1020 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 15.0 10.0 10.0 0.000 0.000 0.330 0.330 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1021 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 35.0 10.0 10.0 0.000 0.000 4.283 4.283 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1022 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 35.0 10.0 10.0 0.000 0.000 0.765 0.765 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1023 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 35.0 10.0 10.0 0.000 0.000 2.807 2.807 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1024 BP-Husky Refining LLC (0448020007) 296027.70 4617056.19 588.6 35.0 10.0 10.0 0.666 0.666 1.331 1.331 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1025 Libbey Glass Inc. (0448010066) 290520.96 4616252.41 592.6 30.0 10.0 10.0 0.169 0.169 0.338 0.338 0.558 0.558 1.080 Yes Yes Yes YesOFFSITE1026 Libbey Glass Inc. (0448010066) 290508.87 4616263.52 592.6 30.0 10.0 10.0 0.159 0.159 0.317 0.317 0.521 0.521 0.982 Yes Yes Yes YesOFFSITE1027 Libbey Glass Inc. (0448010066) 290498.25 4616273.19 592.6 30.0 10.0 10.0 0.177 0.177 0.354 0.354 0.587 0.587 1.247 Yes Yes Yes YesOFFSITE1028 Libbey Glass Inc. (0448010066) 290487.61 4616282.86 592.6 30.0 10.0 10.0 0.136 0.136 0.272 0.272 0.450 0.450 0.679 Yes Yes Yes YesOFFSITE1029 Libbey Glass Inc. (0448010066) 290476.98 4616293.49 592.6 30.0 10.0 10.0 0.139 0.139 0.279 0.279 0.458 0.458 0.719 Yes Yes Yes YesOFFSITE1030 Libbey Glass Inc. (0448010066) 290462.00 4616305.09 592.6 30.0 10.0 10.0 0.156 0.156 0.313 0.313 0.515 0.515 0.812 Yes Yes Yes YesOFFSITE1031 Libbey Glass Inc. (0448010066) 290454.75 4616310.88 592.6 30.0 10.0 10.0 0.176 0.176 0.352 0.352 0.581 0.581 1.084 Yes Yes Yes YesOFFSITE1032 Libbey Glass Inc. (0448010066) 290447.50 4616319.10 592.6 30.0 10.0 10.0 0.174 0.174 0.347 0.347 0.575 0.575 7.920 Yes Yes Yes YesOFFSITE1033 Libbey Glass Inc. (0448010066) 290439.77 4616326.32 592.6 30.0 10.0 10.0 0.172 0.172 0.345 0.345 0.571 0.571 1.070 Yes Yes Yes YesOFFSITE1034 Libbey Glass Inc. (0448010066) 290432.04 4616333.57 592.6 30.0 10.0 10.0 0.174 0.174 0.347 0.347 0.572 0.572 1.075 Yes Yes Yes YesOFFSITE1035 Libbey Glass Inc. (0448010066) 290430.11 4616394.46 592.6 30.0 10.0 10.0 0.176 0.176 0.352 0.352 0.580 0.580 2.640 Yes Yes Yes YesOFFSITE1036 Libbey Glass Inc. (0448010066) 290422.37 4616387.21 592.6 30.0 10.0 10.0 0.100 0.100 0.200 0.200 0.660 0.660 2.750 Yes Yes Yes YesOFFSITE1037 Libbey Glass Inc. (0448010066) 290407.88 4616370.30 592.6 30.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1038 Libbey Glass Inc. (0448010066) 290399.18 4616364.02 592.6 30.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1039 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.202 1.202 0.240 No No Yes YesOFFSITE1040 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.503 1.503 0.301 No No Yes YesOFFSITE1041 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.503 1.503 0.301 No No Yes YesOFFSITE1042 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.202 1.202 0.240 No No Yes YesOFFSITE1043 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.503 1.503 0.301 No No Yes YesOFFSITE1044 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.202 1.202 0.240 No No Yes YesOFFSITE1045 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.202 1.202 0.240 No No Yes YesOFFSITE1046 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.353 1.353 0.541 No No Yes YesOFFSITE1047 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.202 1.202 0.240 No No Yes YesOFFSITE1048 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.052 1.052 0.210 No No Yes YesOFFSITE1049 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.353 1.353 0.271 No No Yes YesOFFSITE1050 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.052 1.052 0.210 No No Yes YesOFFSITE1051 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.503 1.503 0.301 No No Yes YesOFFSITE1052 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.503 1.503 0.301 No No Yes YesOFFSITE1053 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.503 1.503 0.301 No No Yes YesOFFSITE1054 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.353 1.353 0.271 No No Yes YesOFFSITE1055 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.353 1.353 0.271 No No Yes YesOFFSITE1056 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.202 1.202 0.240 No No Yes YesOFFSITE1057 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.653 1.653 0.331 No No Yes YesOFFSITE1058 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.103 1.103 0.221 No No Yes YesOFFSITE1059 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 1.202 1.202 0.240 No No Yes YesOFFSITE1060 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE1061 FCA US LLC - Toledo North Assembly (0448010414 290972.49 4619116.61 589.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE1062 FirstEnergy Generation LLC, Bay Shore Plant (0448 297155.93 4618506.56 580.9 5.0 10.0 10.0 0.365 0.365 0.365 0.365 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1063 FirstEnergy Generation LLC, Bay Shore Plant (0448 297155.93 4618506.56 580.9 5.0 10.0 10.0 0.886 0.886 0.886 0.886 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1064 FirstEnergy Generation LLC, Bay Shore Plant (0448 297155.93 4618506.56 580.9 5.0 10.0 10.0 0.186 0.186 2.018 2.018 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1065 FirstEnergy Generation LLC, Bay Shore Plant (0448 297155.93 4618506.56 580.9 5.0 10.0 10.0 1.550 1.550 1.550 1.550 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1066 FirstEnergy Generation LLC, Bay Shore Plant (0448 297155.93 4618506.56 580.9 5.0 10.0 10.0 0.804 0.804 0.804 0.804 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1067 Hoffman Road Landfill (0448011576) 291397.63 4620215.51 587.7 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1068 Hoffman Road Landfill (0448011576) 291397.63 4620215.51 587.7 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1069 Hoffman Road Landfill (0448011576) 291397.63 4620215.51 587.7 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1070 FCA US LLC- Wrangler Paint Facility (0448011731) 289708.82 4618629.05 591.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No No

Page 301: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Volume Source Model Input Data (Sources sithin 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Release Height

(ft) Sigma Y (ft) Sigma Z (ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE1071 FCA US LLC- Wrangler Paint Facility (0448011731) 289708.82 4618629.05 591.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1072 FCA US LLC- Wrangler Paint Facility (0448011731) 289708.82 4618629.05 591.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1073 FCA US LLC- Wrangler Paint Facility (0448011731) 289708.82 4618629.05 591.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1074 FCA US LLC- Wrangler Paint Facility (0448011731) 289708.82 4618629.05 591.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1075 FCA US LLC- Wrangler Paint Facility (0448011731) 289708.82 4618629.05 591.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1076 FCA US LLC- Wrangler Paint Facility (0448011731) 289708.82 4618629.05 591.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1077 Perstorp Polyols, Inc. (0448010133) 289496.65 4620054.43 591.1 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1078 Perstorp Polyols, Inc. (0448010133) 289496.65 4620054.43 591.1 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1079 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 5.0 10.0 10.0 0.070 0.070 0.405 0.405 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1080 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 35.0 10.0 10.0 1.087 1.087 5.434 5.434 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1081 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 35.0 10.0 10.0 0.203 0.203 1.016 1.016 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1082 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 35.0 10.0 10.0 2.692 2.692 13.459 13.459 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1083 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 35.0 10.0 10.0 2.420 2.420 12.100 12.100 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1084 Toledo Refining Company, LLC. (0448010246) 292157.69 4611093.13 613.6 35.0 10.0 10.0 1.635 1.635 8.174 8.174 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1085 OmniSource Corporation (0448011189) 288470.22 4620548.11 596.8 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1086 OmniSource Corporation (0448011189) 288470.22 4620548.11 596.8 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1087 OmniSource Corporation (0448011189) 288470.22 4620548.11 596.8 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1088 OmniSource Corporation (0448011189) 288470.22 4620548.11 596.8 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1089 THE ANDERSONS, INC. (0448011196) 288608.34 4611924.64 600.9 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1090 THE ANDERSONS, INC. (0448011196) 288608.34 4611924.64 600.9 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1091 THE ANDERSONS, INC. (0448011196) 288608.34 4611924.64 600.9 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1092 THE ANDERSONS, INC. (0448011196) 288608.34 4611924.64 600.9 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1093 THE ANDERSONS, INC. (0448011196) 288608.34 4611924.64 600.9 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1094 THE ANDERSONS, INC. (0448011196) 288608.34 4611924.64 600.9 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1095 THE ANDERSONS, INC. (0448011196) 288608.34 4611924.64 600.9 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1096 NORTH TOLEDO GRAPHICS LLC (0448010300) 288040.96 4620900.87 595.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1097 NORTH TOLEDO GRAPHICS LLC (0448010300) 288040.96 4620900.87 595.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1098 NORTH TOLEDO GRAPHICS LLC (0448010300) 288040.96 4620900.87 595.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1099 NORTH TOLEDO GRAPHICS LLC (0448010300) 288040.96 4620900.87 595.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1100 TRANSFLO Terminal Services, Inc. (0448011937) 289109.24 4611009.76 594.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1101 Evergreen Recycling and Disposal Facility (0387000 292522.11 4608668.92 612.1 5.0 10.0 10.0 0.000 0.000 44.521 44.521 0.000 0.000 0.000 No Yes No YesOFFSITE1102 Evergreen Recycling and Disposal Facility (0387000 292522.11 4608668.92 612.1 5.0 10.0 10.0 0.000 0.000 2.460 2.460 0.000 0.000 53.500 No Yes No YesOFFSITE1103 Evergreen Recycling and Disposal Facility (0387000 292522.11 4608668.92 612.1 5.0 10.0 10.0 0.000 0.000 2.460 2.460 0.000 0.000 53.500 No Yes No YesOFFSITE1104 BOWERS ASPHALT & PAVING, INC (0387040084) 290422.06 4607017.37 618.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1105 Norplas Industries Inc. (0387000362) 287960.55 4607998.59 622.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1106 SHELLY MATERIALS PLANT # 4132 (0448010386) 283127.27 4614472.01 618.4 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1107 American Warming and Ventilating, a division of M 298550.42 4606336.13 607.1 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1108 Decorative Panels International Inc (0448011193) 282413.86 4613073.27 623.9 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1109 FCA US LLC - Toledo Machining Plant (0387040123 288386.79 4603571.95 627.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1110 FCA US LLC - Toledo Machining Plant (0387040123 288386.79 4603571.95 627.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1111 FCA US LLC - Toledo Machining Plant (0387040123 288386.79 4603571.95 627.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1112 HA INTERNATIONAL LLC (0448011215) 280600.63 4610565.60 592.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1113 HA INTERNATIONAL LLC (0448011215) 280600.63 4610565.60 592.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1114 HA INTERNATIONAL LLC (0448011215) 280600.63 4610565.60 592.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1115 HA INTERNATIONAL LLC (0448011215) 280600.63 4610565.60 592.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1116 HA INTERNATIONAL LLC (0448011215) 280600.63 4610565.60 592.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1117 HA INTERNATIONAL LLC (0448011215) 280600.63 4610565.60 592.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1118 HA INTERNATIONAL LLC (0448011215) 280600.63 4610565.60 592.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1119 HA INTERNATIONAL LLC (0448011215) 280600.63 4610565.60 592.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1120 The Andersons, Inc. (0448031076) 277764.15 4605250.22 634.1 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1121 The Andersons, Inc. (0448031076) 277764.15 4605250.22 634.1 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1122 Bulk Molding Compounds, Inc. (0387040001) 279353.55 4603134.11 633.4 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1123 Bulk Molding Compounds, Inc. (0387040001) 279353.55 4603134.11 633.4 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1124 Graymont Dolime (OH), Inc. (0362000079) 303860.85 4597980.26 621.1 5.0 10.0 10.0 0.091 0.091 0.607 0.607 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1125 Graymont Dolime (OH), Inc. (0362000079) 303860.85 4597980.26 621.1 5.0 10.0 10.0 0.138 0.138 1.332 1.332 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1126 Graymont Dolime (OH), Inc. (0362000079) 303860.85 4597980.26 621.1 5.0 10.0 10.0 0.055 0.055 0.297 0.297 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1127 Graymont Dolime (OH), Inc. (0362000079) 303860.85 4597980.26 621.1 5.0 10.0 10.0 0.106 0.106 0.322 0.322 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1128 Graymont Dolime (OH), Inc. (0362000079) 303860.85 4597980.26 621.1 5.0 10.0 10.0 0.214 0.214 0.266 0.266 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1129 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 5.0 10.0 10.0 16.756 16.756 16.756 16.756 15.799 15.799 0.000 Yes Yes Yes NoOFFSITE1130 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 5.0 10.0 10.0 17.514 17.514 17.514 17.514 16.584 16.584 0.000 Yes Yes Yes NoOFFSITE1131 Johns Manville / Plant #01 - wtv1 (0448000012) 273939.15 4601325.94 631.4 5.0 10.0 10.0 0.577 0.577 0.577 0.577 0.000 0.000 0.000 Yes Yes Yes NoOFFSITE1132 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.275 0.275 2.023 2.023 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1133 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.648 0.648 4.285 4.285 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1134 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.010 0.010 0.028 0.028 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1135 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.010 0.010 0.028 0.028 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1136 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.059 0.059 0.140 0.140 0.000 0.000 0.000 Yes Yes Yes Yes

Page 302: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Volume Source Model Input Data (Sources sithin 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Release Height

(ft) Sigma Y (ft) Sigma Z (ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE1137 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 2.235 2.235 2.235 2.235 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1138 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.388 0.388 0.961 0.961 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1139 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.388 0.388 0.961 0.961 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1140 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.388 0.388 0.961 0.961 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1141 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.933 0.933 4.063 4.063 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1142 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.933 0.933 4.063 4.063 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1143 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 1.500 1.500 1.500 1.500 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1144 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.128 0.128 0.268 0.268 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1145 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.128 0.128 0.268 0.268 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1146 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1147 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1148 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1149 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1150 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1151 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1152 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1153 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1154 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1155 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1156 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1157 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0 302362.90 4593267.70 633.3 5.0 10.0 10.0 0.224 0.224 0.413 0.413 0.000 0.000 0.000 Yes Yes Yes YesOFFSITE1158 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1159 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1160 REXAM Beverage Can Co (0448002007) 270313.17 4604033.74 637.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1161 Kokosing Materials - Plant 521 (0372002004) 303873.49 4590756.50 633.1 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1162 Materion Brush Inc. (0362000009) 314987.71 4595346.37 596.8 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1163 Port Clinton Landfill (0362010118) 331019.44 4598773.52 576.1 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1164 Carmeuse Lime Inc Millersville Operations (037200 308908.24 4577351.19 682.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1165 Carmeuse Lime Inc Millersville Operations (037200 308908.24 4577351.19 682.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1166 Carmeuse Lime Inc Millersville Operations (037200 308908.24 4577351.19 682.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1167 Carmeuse Lime Inc Millersville Operations (037200 308908.24 4577351.19 682.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1168 Carmeuse Lime Inc Millersville Operations (037200 308908.24 4577351.19 682.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1169 Carmeuse Lime Inc Millersville Operations (037200 308908.24 4577351.19 682.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1170 P.H. Glatfelter Co. - Fremont Facility (0372030100) 320387.34 4581532.92 625.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1171 P.H. Glatfelter Co. - Fremont Facility (0372030100) 320387.34 4581532.92 625.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1172 Style Crest Enterprises, Inc. (0372030210) 323218.14 4582265.41 615.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1173 Style Crest Enterprises, Inc. (0372030210) 323218.14 4582265.41 615.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1174 Style Crest Enterprises, Inc. (0372030210) 323218.14 4582265.41 615.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1175 WORTHINGTON STEEL (0326000076) 247120.16 4607312.75 732.9 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1176 WORTHINGTON STEEL (0326000076) 247120.16 4607312.75 732.9 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1177 WORTHINGTON STEEL (0326000076) 247120.16 4607312.75 732.9 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1178 Charter Steel (0387000376) 297129.65 4568812.83 717.1 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1179 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1180 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1181 Rexam Beverage Can Company (0372030005) 322441.36 4578087.32 592.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1182 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 179.600 179.600 2362.500 No No Yes YesOFFSITE1183 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE1184 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE1185 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE1186 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes YesOFFSITE1187 NorthStar Bluescope Steel, LLC (0326000073) 246093.96 4605248.76 740.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 9.830 9.830 53.500 No No Yes YesOFFSITE1188 VIENNA JUNCTION LANDFILL 291000.00 4625000.00 584.8 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1189 J.R. WHITING CO 296440.00 4629490.00 580.0 5.0 10.0 10.0 0.000 0.000 0.821 0.821 7.451 7.451 1.198 No Yes Yes YesOFFSITE1190 STONECO INC 278652.00 4625040.00 679.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1191 STONECO INC DENNISTON QUARRY 298000.00 4640600.00 602.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1192 ADM GRAIN CO 270766.00 4627257.00 691.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1193 Gerdau MacSteel Monroe 304524.00 4640317.00 576.4 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No YesOFFSITE1194 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 581.5 5.0 10.0 10.0 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE1195 DETROIT EDISON COMPANY 305350.00 4640200.00 581.5 5.0 10.0 10.0 0.098 0.098 0.098 0.098 1.395 1.395 0.300 Yes Yes Yes YesOFFSITE1196 MICHIGAN PAVING & MATERIALS 304500.00 4640700.00 582.1 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1197 J A JONES ENVIRONMENTAL SERVICES 304600.00 4641500.00 572.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1198 SPARTAN STEEL COATING 305095.00 4647120.00 592.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1199 THE DTE ELECTRIC COMPANY - FERMI ENERGY CEN 312850.00 4647650.00 580.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1200 HOLCIM (US), INC 279800.00 4652300.00 669.8 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1201 STONECO NEWPORT 314800.00 4653800.00 581.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1202 GREAT LAKES AGGREGATES, L.L.C. - SYLVANIA MIN 312000.00 4658000.00 589.3 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No No

Page 303: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Volume Source Model Input Data (Sources sithin 50km of IU Site) (NAD83, Zone 17)Potential Emissions (lb/hr)

Source ID Source DescriptionEasting (X)

(m)Northing (Y)

(m)

Base Elevation

(ft)

Release Height

(ft) Sigma Y (ft) Sigma Z (ft) PM25PM25

(annual) PM10PM-10

(annual)NOx

(annual) NO2 CO

Include in PM25

Model?

Include in PM10

Model?

Include in NO2/NOx

Model?Include in

CO Model?OFFSITE1203 STONECO, INC 298000.00 4640600.00 602.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1204 COUNTRYMARK COOPERATIVE, INC 270766.00 4627257.00 691.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1205 IKO MONROE, INC 300200.00 4644200.00 598.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1206 GUARDIAN INDUSTRIES 304915.00 4662490.00 614.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No Yes NoOFFSITE1207 MICHIGAN AGRICULTURAL COMMODITIES 263500.00 4634500.00 690.9 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1208 MICHIGAN AGRICULTURAL COMMODITIES 263500.00 4634500.00 690.9 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1209 WACKER CHEMICAL CORP 255600.00 4648000.00 768.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1210 WACKER CHEMICAL CORP 255600.00 4648000.00 768.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1211 ADRIAN ENERGY ASSOICATES 251300.00 4642135.00 807.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1212 ADRIAN LANDFILL 251300.00 4642135.00 807.6 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1213 Faurecia Interior Systems Saline, LLC 271557.00 4627931.00 684.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1214 AUTOMOTIVE COMPONENTS HOLDINGS, LLC 271557.00 4627931.00 684.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1215 Georgia-Pacific Corrugated II LLC 278400.00 4663100.00 703.1 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1216 B.O.P. FEDERAL CORRECTIONAL INSTITUTE 279050.00 4663500.00 699.9 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1217 GS Materials, LLC 253000.00 4646500.00 708.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1218 G S MATERIALS, LLC 253000.00 4646500.00 708.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1219 CARLETON FARMS LANDFILL 299500.00 4662700.00 640.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 36.260 No No No YesOFFSITE1220 CARLETON FARMS LANDFILL 299500.00 4662700.00 640.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 48.459 No No No YesOFFSITE1221 CARLETON FARMS LANDFILL 299500.00 4662700.00 640.2 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No YesOFFSITE1222 U S SILICA CO 315500.00 4658500.00 587.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1223 U S SILICA CO 315500.00 4658500.00 587.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1224 U S SILICA CO 315500.00 4658500.00 587.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1225 U S SILICA CO 315500.00 4658500.00 587.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1226 U S SILICA CO 315500.00 4658500.00 587.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1227 U S SILICA CO 315500.00 4658500.00 587.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1228 U S SILICA CO 315500.00 4658500.00 587.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1229 U S SILICA CO 315500.00 4658500.00 587.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1230 U S SILICA CO 315500.00 4658500.00 587.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1231 U S SILICA CO 315500.00 4658500.00 587.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1232 U S SILICA CO 315500.00 4658500.00 587.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1233 CITY SAND & LANDFILL INC 293500.00 4664600.00 652.5 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1234 FLAT ROCK METAL INC 310089.00 4663986.00 590.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1235 FLAT ROCK METAL INC 310089.00 4663986.00 590.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1236 FLAT ROCK METAL INC 310089.00 4663986.00 590.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1237 FLAT ROCK METAL INC 310089.00 4663986.00 590.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1238 FLAT ROCK METAL INC 310089.00 4663986.00 590.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1239 FLAT ROCK METAL INC 310089.00 4663986.00 590.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No NoOFFSITE1240 FLAT ROCK METAL INC 310089.00 4663986.00 590.0 5.0 10.0 10.0 0.000 0.000 0.000 0.000 0.000 0.000 0.000 No No No No

Missing velocity or zero velocity set to 1 ft/sec. 893.055Missing diameter or zero velocity set to 1 ft.Missing temp or zero temp set to 70F.Missing height or zero height set to 5 ft. Cooling towers set to 35'.Base elevations calculated with AERMAP.Inititial dispersion characteristics set to 10ft.Bold italics indicate PM10 increment consuming source. Red bold italics indicate PM2.5 increment consuming source.All sources conservatively assumed to consume NO2 increment.

Page 304: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx CO0448011575 TOLEDO SHREDDING LLC (0448011575) F002 Roadway emissions 293963.00 4616843.00 0.50 9.91 No 3.16 3.16 0.00 0.000448011575 TOLEDO SHREDDING LLC (0448011575) P902 Stack No. 1, 2 294058.47 4616773.57 0.49 9.78 No 2.28 2.28 0.00 0.000448011575 TOLEDO SHREDDING LLC (0448011575) P901 Material handling emissions 294096.00 4616751.00 0.50 9.95 No 2.64 2.64 0.00 0.000448011575 Total 0.49 9.78 8.08 8.08 0.00 0.00 Y Y Y Y Screen Screen Screen Screen NA NA NA NA No No No No0448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) F005 Animal Feed Loading for Railcar 291939.00 4615597.00 1.98 39.52 No 1.04 2.75 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) F005 General exhaust for animal feed building 291939.00 4615597.00 1.98 39.52 No 1.04 2.75 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) F006 Truck Loading Emissions Operation 291939.00 4615597.00 1.98 39.52 No 0.78 2.07 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) F006 General exhaust for animal feed building 291939.00 4615597.00 1.98 39.52 No 0.78 2.07 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) F011 Fugitive emissions from 48 building white wheat s 291939.00 4615597.00 1.98 39.52 No 0.07 0.17 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) F012 Fugitive emissions from 48 building white wheat s 291939.00 4615597.00 1.98 39.52 No 0.04 0.11 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) F013 Ship / Barge Wheat Unloading 291939.00 4615597.00 1.98 39.52 No 0.28 0.72 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P009 Grain Screening and Cleaning 291939.00 4615597.00 1.98 39.52 No 0.45 0.12 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P013 'A' and 'B' Pneu-2 Exhaust 291939.00 4615597.00 1.98 39.52 No 0.59 1.56 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P013 'A' and 'B' Pneu-3 Exhaust 291939.00 4615597.00 1.98 39.52 No 0.59 1.56 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P013 A pat rec exhaust 291939.00 4615597.00 1.98 39.52 No 0.59 1.56 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P013 A bal rec exhaust 291939.00 4615597.00 1.98 39.52 No 0.59 1.56 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P013 'A' & 'B' Flour Mill Building 55 transfer 291939.00 4615597.00 1.98 39.52 No 0.59 1.56 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P014 'A' and 'B' Pneu-1 Exhaust 291939.00 4615597.00 1.98 39.52 No 0.59 1.56 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P014 'A' and 'B' Pneu-2 Exhaust 291939.00 4615597.00 1.98 39.52 No 0.59 1.56 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P014 'A' and 'B' Pneu-3 Exhaust 291939.00 4615597.00 1.98 39.52 No 0.59 1.56 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P014 Flour Mill 'B' pat rec 291939.00 4615597.00 1.98 39.52 No 0.59 1.56 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P014 'A' & 'B' Flour Mill Building 55 transfer 291939.00 4615597.00 1.98 39.52 No 0.59 1.56 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P015 Railcar and Truck Flour Loading 85 Building Filter 291939.00 4615597.00 1.98 39.52 No 0.22 0.57 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P015 Railcar Flour Loading 291939.00 4615597.00 1.98 39.52 No 0.22 0.57 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P015 Truck Flour Loading Filter Exhaust 291939.00 4615597.00 1.98 39.52 No 0.22 0.57 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P016 Grain Handling 291939.00 4615597.00 1.98 39.52 No 2.71 11.77 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P900 Truck Dump 291939.00 4615597.00 1.98 39.52 No 0.94 4.07 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P901 Railcar Unloading Tracks 11 / 12 1946 elevator 291939.00 4615597.00 1.98 39.52 No 4.03 10.69 0.00 0.000448010023 Mondelez Global LLC - Toledo Flour Mill (0448010023) P901b Railcar Unloading Tracks 8 / 9 1930 elevator 291939.00 4615597.00 1.98 39.52 No 0.00 0.00 0.00 0.000448010023 Total 1.98 39.52 18.68 54.60 0.00 0.00 Y Y N Y Model Model NA Screen NA NA Screen NA Yes Yes No No0448010737 City of Toledo, Division of Water Reclamation (0448010737) P109 56.1 MMBtu/hr Combustion Turbine 293513.18 4618147.23 1.76 35.30 Yes 5.65 5.65 78.84 127.900448010737 City of Toledo, Division of Water Reclamation (0448010737) HRSG 65.3 MMBtu/hr HRSG 293513.18 4618147.23 1.76 35.30 Yes 2.15 2.15 53.87 32.020448010737 City of Toledo, Division of Water Reclamation (0448010737) P101 Gen#1 293513.18 4618147.23 1.76 35.30 Yes 0.01 0.01 0.41 0.020448010737 City of Toledo, Division of Water Reclamation (0448010737) P105 Gen#5 293513.18 4618147.23 1.76 35.30 Yes 0.01 0.01 27.86 65.790448010737 City of Toledo, Division of Water Reclamation (0448010737) P106 Gen#6 293513.18 4618147.23 1.76 35.30 Yes 0.01 0.01 27.86 65.790448010737 City of Toledo, Division of Water Reclamation (0448010737) P102 293513.18 4618147.23 1.76 35.30 Yes 0.00 0.00 0.18 0.130448010737 City of Toledo, Division of Water Reclamation (0448010737) P103 293513.18 4618147.23 1.76 35.30 Yes 0.00 0.00 0.18 0.180448010737 City of Toledo, Division of Water Reclamation (0448010737) P104 293513.18 4618147.23 1.76 35.30 Yes 0.00 0.00 0.07 0.060448010737 Total 1.76 35.30 7.82 7.82 189.27 291.88 Y Y N Y Screen Screen NA Model NA NA Model NA No No Yes Yes0448020014 Chemtrade Refinery Solutions Limited Partnership (0448020014) B001 B001 295618.61 4617346.77 2.10 41.99 Yes 0.18 0.18 4.16 7.010448020014 Chemtrade Refinery Solutions Limited Partnership (0448020014) B002 B002 295618.61 4617346.77 2.10 41.99 Yes 0.13 0.13 3.64 6.130448020014 Chemtrade Refinery Solutions Limited Partnership (0448020014) P001 P001 295618.61 4617346.77 2.10 41.99 Yes 14.13 21.74 25.84 32.460448020014 Chemtrade Refinery Solutions Limited Partnership (0448020014) P002 P002 295618.61 4617346.77 2.10 41.99 Yes 3.71 5.71 16.29 18.050448020014 Total 2.10 41.99 18.15 27.76 49.93 63.64 Y Y N Y Model Model NA Model NA NA Model NA Yes Yes Yes Yes0448020007 BP-Husky Refining LLC (0448020007) B008 B008 Stack Iso 2 Feed Heater 296027.70 4617056.19 2.38 47.50 Yes 8.53 8.53 19.86 16.680448020007 BP-Husky Refining LLC (0448020007) B009 B010 Stack Common Stack for Iso 2 Splitter and IS 296027.70 4617056.19 2.38 47.50 Yes 9.64 9.64 48.59 10.040448020007 BP-Husky Refining LLC (0448020007) B010 B010 Stack Common Stack for Iso 2 Splitter and IS 296027.70 4617056.19 2.38 47.50 Yes 9.64 9.64 61.19 12.570448020007 BP-Husky Refining LLC (0448020007) B015 Conv.Htr.St 296027.70 4617056.19 2.38 47.50 Yes 24.53 24.53 292.16 109.620448020007 BP-Husky Refining LLC (0448020007) B017 B017 Stack Coker 2 Heater 296027.70 4617056.19 2.38 47.50 Yes 6.31 6.31 12.42 10.430448020007 BP-Husky Refining LLC (0448020007) B019 B019 Stack Crude/ Vac 2 Furnace 296027.70 4617056.19 2.38 47.50 Yes 22.60 22.60 262.80 56.180448020007 BP-Husky Refining LLC (0448020007) B022 Conv.Htr.St 296027.70 4617056.19 2.38 47.50 Yes 6.75 6.75 30.63 25.730448020007 BP-Husky Refining LLC (0448020007) B029 B029 Stack ADHT Furnace 296027.70 4617056.19 2.38 47.50 Yes 0.74 0.74 7.01 8.230448020007 BP-Husky Refining LLC (0448020007) B030 B030 Stack BGOT Furnace 296027.70 4617056.19 2.38 47.50 Yes 1.31 1.31 17.65 16.030448020007 BP-Husky Refining LLC (0448020007) B031 Conv.Htr.St 296027.70 4617056.19 2.38 47.50 Yes 3.58 3.58 39.86 39.520448020007 BP-Husky Refining LLC (0448020007) B032 B032 Stack Coker 3 Furnace 296027.70 4617056.19 2.38 47.50 Yes 5.47 5.47 105.78 60.440448020007 BP-Husky Refining LLC (0448020007) B033 B033 Stack B-GOT East Furnace 296027.70 4617056.19 2.38 47.50 Yes 1.10 1.10 2.93 11.830448020007 BP-Husky Refining LLC (0448020007) B034 B034 Stack East Alstom Boiler 296027.70 4617056.19 2.38 47.50 Yes 11.52 11.52 55.67 168.540448020007 BP-Husky Refining LLC (0448020007) B035 B035 Stack West Alstom Boiler 296027.70 4617056.19 2.38 47.50 Yes 11.52 11.52 55.67 168.540448020007 BP-Husky Refining LLC (0448020007) B036 Reformer 3 Heater Stack 296027.70 4617056.19 2.38 47.50 Yes 17.08 17.08 102.29 81.470448020007 BP-Husky Refining LLC (0448020007) B903 Stack for Asphalt Tank Heaters for Tanks T175 (50 296027.70 4617056.19 2.38 47.50 Yes 0.15 0.15 1.93 1.620448020007 BP-Husky Refining LLC (0448020007) P003 East Hydrocarbon Flare vent 296027.70 4617056.19 2.38 47.50 Yes 0.65 0.65 5.89 32.030448020007 BP-Husky Refining LLC (0448020007) P004 West Hydrocarbon Flare Vent 296027.70 4617056.19 2.38 47.50 Yes 2.12 2.12 19.36 105.340448020007 BP-Husky Refining LLC (0448020007) P007 COB Stack. Normal operating exhaust from FCCU/ 296027.70 4617056.19 2.38 47.50 Yes 29.30 29.30 176.13 19.390448020007 BP-Husky Refining LLC (0448020007) P007 FCC Bypass Stack. Emergency bypass of CO Boiler 296027.70 4617056.19 2.38 47.50 Yes 29.30 29.30 1.78 0.200448020007 BP-Husky Refining LLC (0448020007) P009 SRU 1 Stack 296027.70 4617056.19 2.38 47.50 Yes 0.23 0.23 3.03 2.550448020007 BP-Husky Refining LLC (0448020007) P037 SRU 2 and 3 (P037) Stack from SRU 2 and 3 Therm 296027.70 4617056.19 2.38 47.50 Yes 2.63 2.63 19.27 11.830448020007 BP-Husky Refining LLC (0448020007) P048 P048 Stack - knock motors 296027.70 4617056.19 2.38 47.50 Yes 0.15 0.15 1.96 1.260448020007 BP-Husky Refining LLC (0448020007) P049 East Acid Gas Flare vent 296027.70 4617056.19 2.38 47.50 Yes 0.24 0.24 2.15 11.700448020007 BP-Husky Refining LLC (0448020007) P050 TRP SRU Acid Gas Flare vent. For rare emergency 296027.70 4617056.19 2.38 47.50 Yes 0.24 0.24 2.15 11.700448020007 BP-Husky Refining LLC (0448020007) P051 SRU #1 Acid Gas Flare 296027.70 4617056.19 2.38 47.50 Yes 0.22 0.22 1.97 10.730448020007 BP-Husky Refining LLC (0448020007) P803 Regenerator vent from Reformer 3 296027.70 4617056.19 2.38 47.50 Yes 0.00 0.00 0.00 0.250448020007 BP-Husky Refining LLC (0448020007) P017 K2 Cutting 296027.70 4617056.19 2.38 47.50 Yes 0.40 0.43 0.00 0.050448020007 BP-Husky Refining LLC (0448020007) P036 K3 Cutting 296027.70 4617056.19 2.38 47.50 Yes 1.57 1.72 0.00 0.160448020007 BP-Husky Refining LLC (0448020007) P044 P044 diesel pump #1 exhaust 296027.70 4617056.19 2.38 47.50 Yes 0.08 0.08 1.02 0.110448020007 BP-Husky Refining LLC (0448020007) P045 P045 diesel pump #2 exhaust 296027.70 4617056.19 2.38 47.50 Yes 0.08 0.08 1.02 0.110448020007 BP-Husky Refining LLC (0448020007) P803 Outdoor Refinery Process Unit Piping 296027.70 4617056.19 2.38 47.50 Yes 0.00 0.00 0.01 1.150448020007 BP-Husky Refining LLC (0448020007) F001 Roads/Park 296027.70 4617056.19 2.38 47.50 Yes 0.54 4.59 0.00 0.00

Page 305: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx CO0448020007 BP-Husky Refining LLC (0448020007) F005 F005 Coke Handling 296027.70 4617056.19 2.38 47.50 Yes 0.53 3.62 0.00 0.000448020007 BP-Husky Refining LLC (0448020007) F006 F006 Coke Crushing 296027.70 4617056.19 2.38 47.50 Yes 0.74 1.45 0.00 0.000448020007 BP-Husky Refining LLC (0448020007) P055 P055 Cooling Tower 1 296027.70 4617056.19 2.38 47.50 Yes 9.38 18.76 0.00 0.000448020007 BP-Husky Refining LLC (0448020007) P056 P056 Cooling Tower 3 296027.70 4617056.19 2.38 47.50 Yes 1.68 3.35 0.00 0.000448020007 BP-Husky Refining LLC (0448020007) P057 P057 Cooling Tower 4 296027.70 4617056.19 2.38 47.50 Yes 6.15 12.29 0.00 0.000448020007 BP-Husky Refining LLC (0448020007) P058 P058 DHT Cooling Tower 296027.70 4617056.19 2.38 47.50 Yes 2.92 5.83 0.00 0.000448020007 Total 2.38 47.50 229.61 257.74 1352.18 1006.01 Y N N Y Model NA NA Model NA Model Model NA Yes Yes Yes Yes448020102 Oregon Clean Energy CT1 Cooling Tower Cell 1 296389.28 4615758.47 2.72 54.39 Yes 0.28 0.28 0.00 0.00448020102 Oregon Clean Energy CT16 Cooling Tower Cell 16 296389.11 4615744.68 2.72 54.46 Yes 0.28 0.28 0.00 0.00448020102 Oregon Clean Energy CT2 Cooling Tower Cell 2 296404.77 4615758.47 2.73 54.70 Yes 0.28 0.28 0.00 0.00448020102 Oregon Clean Energy CT15 Cooling Tower Cell 15 296404.84 4615744.67 2.74 54.76 Yes 0.28 0.28 0.00 0.00448020102 Oregon Clean Energy CT3 Cooling Tower Cell 3 296419.89 4615758.25 2.75 54.99 Yes 0.28 0.28 0.00 0.00448020102 Oregon Clean Energy CT14 Cooling Tower Cell 14 296419.90 4615744.35 2.75 55.06 Yes 0.28 0.28 0.00 0.00448020102 Oregon Clean Energy CT4 Cooling Tower Cell 4 296435.54 4615758.04 2.76 55.30 Yes 0.28 0.28 0.00 0.00448020102 Oregon Clean Energy CT13 Cooling Tower Cell 13 296435.52 4615744.35 2.77 55.36 Yes 0.28 0.28 0.00 0.00448020102 Oregon Clean Energy CT5 Cooling Tower Cell 5 296451.20 4615758.15 2.78 55.60 Yes 0.28 0.28 0.00 0.00448020102 Oregon Clean Energy CT12 Cooling Tower Cell 12 296451.20 4615744.35 2.78 55.66 Yes 0.28 0.28 0.00 0.00448020102 Oregon Clean Energy CT6 Cooling Tower Cell 6 296466.87 4615758.15 2.80 55.91 Yes 0.28 0.28 0.00 0.00448020102 Oregon Clean Energy CT11 Cooling Tower Cell 11 296466.87 4615744.35 2.80 55.97 Yes 0.28 0.28 0.00 0.00448020102 Oregon Clean Energy CT7 Cooling Tower Cell 7 296482.55 4615758.09 2.81 56.21 Yes 0.28 0.28 0.00 0.00448020102 Oregon Clean Energy CT10 Cooling Tower Cell 10 296482.37 4615744.40 2.81 56.27 Yes 0.28 0.28 0.00 0.00448020102 Oregon Clean Energy CT8 Cooling Tower Cell 8 296498.15 4615758.09 2.83 56.51 Yes 0.28 0.28 0.00 0.00448020102 Oregon Clean Energy CT8 Cooling Tower Cell 9 296498.16 4615744.46 2.83 56.58 Yes 0.28 0.28 0.00 0.00448020102 Oregon Clean Energy HRGN HRGN 296560.98 4615757.31 2.89 57.74 Yes 58.70 58.70 87.52 87.52448020102 Oregon Clean Energy AUXB Aux Boiler 296560.98 4615757.00 2.89 57.74 Yes 0.00 0.00 0.00 8.68448020102 Oregon Clean Energy HRGS HRGS 296560.71 4615714.43 2.90 57.93 Yes 58.70 58.70 87.52 87.52448020102 Total 2.72 54.39 121.95 121.95 175.05 183.73 Y N N N Model NA NA NA NA Model Model Model Yes Yes Yes Yes448020102b Oregon Energy Center GT1 Turbine 1 297092.82 4615514.53 3.46 69.23 Yes 65.26 65.26 106.43 65.26448020102b Oregon Energy Center GT2 Turbine 2 297092.75 4615560.13 3.45 69.00 Yes 65.26 65.26 106.43 65.26448020102b Oregon Energy Center AUXBLR Aux Boiler 297092.83 4615510.44 3.46 69.25 Yes 1.31 1.31 3.33 9.11448020102b Oregon Energy Center CT1 Cooling Tower Cell 1 297055.11 4615415.73 3.45 69.04 Yes 0.16 0.41 0.00 0.00448020102b Oregon Energy Center CT2 Cooling Tower Cell 2 297065.11 4615415.73 3.46 69.23 Yes 0.16 0.41 0.00 0.00448020102b Oregon Energy Center CT3 Cooling Tower Cell 3 297077.19 4615427.69 3.47 69.40 Yes 0.16 0.41 0.00 0.00448020102b Oregon Energy Center CT4 Cooling Tower Cell 4 297089.37 4615439.78 3.48 69.56 Yes 0.16 0.41 0.00 0.00448020102b Oregon Energy Center CT5 Cooling Tower Cell 5 297101.40 4615451.85 3.49 69.73 Yes 0.16 0.41 0.00 0.00448020102b Oregon Energy Center CT6 Cooling Tower Cell 6 297113.35 4615463.88 3.49 69.89 Yes 0.16 0.41 0.00 0.00448020102b Oregon Energy Center CT7 Cooling Tower Cell 7 297125.42 4615475.82 3.50 70.06 Yes 0.16 0.41 0.00 0.00448020102b Oregon Energy Center CT8 Cooling Tower Cell 8 297137.62 4615488.19 3.51 70.23 Yes 0.16 0.41 0.00 0.00448020102b Oregon Energy Center CT9 Cooling Tower Cell 9 297149.52 4615500.22 3.52 70.40 Yes 0.16 0.41 0.00 0.00448020102b Oregon Energy Center CT10 Cooling Tower Cell 10 297161.65 4615512.27 3.53 70.58 Yes 0.16 0.41 0.00 0.00448020102b Oregon Energy Center EGEN Emergency Engine 297173.78 4615524.40 3.54 70.75 Yes 2.19 2.19 70.52 38.54448020102b Oregon Energy Center FP Fire Water Pump 297113.78 4615522.08 3.48 69.60 Yes 0.44 0.44 8.63 7.58448020102b Total 3.45 69.00 136.05 138.54 295.34 185.76 N N N N NA NA NA NA Model Model Model Model Yes Yes Yes Yes0448010066 Libbey Glass Inc. (0448010066) B004 Boiler # 1 290500.34 4616413.27 3.25 64.91 Yes 0.90 0.90 6.54 4.060448010066 Libbey Glass Inc. (0448010066) B005 Boiler # 2 290500.34 4616413.27 3.25 64.91 Yes 0.90 0.90 6.54 4.060448010066 Libbey Glass Inc. (0448010066) B006 Boiler # 3 290500.34 4616413.27 3.25 64.91 Yes 0.90 0.90 6.54 4.060448010066 Libbey Glass Inc. (0448010066) P003 27-B 290500.34 4616413.27 3.25 64.91 Yes 14.89 14.89 67.50 0.100448010066 Libbey Glass Inc. (0448010066) P005 27-D 290500.34 4616413.27 3.25 64.91 Yes 36.79 36.79 39.11 0.060448010066 Libbey Glass Inc. (0448010066) P007 27-G 290500.34 4616413.27 3.25 64.91 Yes 27.59 27.59 202.79 4.680448010066 Libbey Glass Inc. (0448010066) P011 Deco Line 1 290500.34 4616413.27 3.25 64.91 Yes 0.12 0.12 4.40 1.320448010066 Libbey Glass Inc. (0448010066) P022 27-F 290500.34 4616413.27 3.25 64.91 Yes 37.93 37.93 122.64 3.290448010066 Libbey Glass Inc. (0448010066) P010 Cartons#1 290500.34 4616413.27 3.25 64.91 Yes 24.09 24.09 0.00 0.000448010066 Libbey Glass Inc. (0448010066) F003 FormingVent 290500.34 4616413.27 3.25 64.91 Yes 1.48 1.48 2.45 4.730448010066 Libbey Glass Inc. (0448010066) F004 FormingVent 290500.34 4616413.27 3.25 64.91 Yes 1.39 1.39 2.28 4.300448010066 Libbey Glass Inc. (0448010066) F007 FormingVent 290500.34 4616413.27 3.25 64.91 Yes 1.55 1.55 2.57 5.460448010066 Libbey Glass Inc. (0448010066) F009 FormingVent 290500.34 4616413.27 3.25 64.91 Yes 1.19 1.19 1.97 2.980448010066 Libbey Glass Inc. (0448010066) F010 FormingVent 290500.34 4616413.27 3.25 64.91 Yes 1.22 1.22 2.01 3.150448010066 Libbey Glass Inc. (0448010066) F011 FormingVent 290500.34 4616413.27 3.25 64.91 Yes 1.37 1.37 2.26 3.560448010066 Libbey Glass Inc. (0448010066) F012 FormingVent 290500.34 4616413.27 3.25 64.91 Yes 1.54 1.54 2.55 4.750448010066 Libbey Glass Inc. (0448010066) F013 FormingVent 290500.34 4616413.27 3.25 64.91 Yes 1.52 1.52 2.52 34.690448010066 Libbey Glass Inc. (0448010066) F014 FormingVent 290500.34 4616413.27 3.25 64.91 Yes 1.51 1.51 2.50 4.690448010066 Libbey Glass Inc. (0448010066) F015 FormingVent 290500.34 4616413.27 3.25 64.91 Yes 1.52 1.52 2.51 4.710448010066 Libbey Glass Inc. (0448010066) F019 FormingVent 290500.34 4616413.27 3.25 64.91 Yes 1.54 1.54 2.54 11.560448010066 Libbey Glass Inc. (0448010066) F020 FormingVent 290500.34 4616413.27 3.25 64.91 Yes 0.88 0.88 2.89 12.050448010066 Libbey Glass Inc. (0448010066) P007 290500.34 4616413.27 3.25 64.91 Yes 2.00 2.00 9.69 0.520448010066 Libbey Glass Inc. (0448010066) P010 290500.34 4616413.27 3.25 64.91 Yes 0.11 0.11 0.00 0.000448010066 Total 3.25 64.91 162.94 162.94 494.78 118.74 N N N N NA NA NA NA Model Model Model Model Yes Yes Yes Yes0448020033 MARATHON PETROLEUM CO LP (0448020033) J001 VCU 296126.59 4614028.58 3.36 67.17 No 0.00 0.00 0.86 4.680448020033 Total 3.36 67.17 0.00 0.00 0.86 4.68 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0448020006 FirstEnergy Generation LLC, Bay Shore Plant (0448020006) B005 B005 297155.93 4618506.56 4.01 80.19 Yes 49.67 49.67 0.00 0.000448020006 FirstEnergy Generation LLC, Bay Shore Plant (0448020006) B006 B006 297155.93 4618506.56 4.01 80.19 Yes 194.38 264.25 2318.33 1545.260448020006 FirstEnergy Generation LLC, Bay Shore Plant (0448020006) P001 P001 297155.93 4618506.56 4.01 80.19 Yes 0.13 0.13 7.62 0.500448020006 FirstEnergy Generation LLC, Bay Shore Plant (0448020006) F010 P001 297155.93 4618506.56 4.01 80.19 Yes 0.82 8.84 0.00 0.000448020006 FirstEnergy Generation LLC, Bay Shore Plant (0448020006) F001 Fugitive 297155.93 4618506.56 4.01 80.19 Yes 1.60 1.60 0.00 0.000448020006 FirstEnergy Generation LLC, Bay Shore Plant (0448020006) F008 Fugitive 297155.93 4618506.56 4.01 80.19 Yes 3.88 3.88 0.00 0.000448020006 FirstEnergy Generation LLC, Bay Shore Plant (0448020006) F010 Fugitive 297155.93 4618506.56 4.01 80.19 Yes 12.80 12.80 0.00 0.000448020006 FirstEnergy Generation LLC, Bay Shore Plant (0448020006) F011 Fugitive 297155.93 4618506.56 4.01 80.19 Yes 6.79 6.79 0.00 0.00

Page 306: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx CO0448020006 FirstEnergy Generation LLC, Bay Shore Plant (0448020006) F012&14 297155.93 4618506.56 4.01 80.19 Yes 3.52 3.52 0.00 0.000448020006 Total 4.01 80.19 273.57 351.48 2325.96 1545.76 N N N N NA NA NA NA Model Model Model Model Yes Yes Yes Yes0448010414 FCA US LLC - Toledo North Assembly (0448010414) B008 EE01 290346.00 4619298.00 4.47 89.38 Yes 1.07 1.07 7.01 11.870448010414 FCA US LLC - Toledo North Assembly (0448010414) B009 EE02 290346.00 4619298.00 4.47 89.38 Yes 1.07 1.07 7.01 11.870448010414 FCA US LLC - Toledo North Assembly (0448010414) B010 EE03 290346.00 4619298.00 4.47 89.38 Yes 1.07 1.07 7.01 11.870448010414 FCA US LLC - Toledo North Assembly (0448010414) B011 290346.00 4619298.00 4.47 89.38 Yes 0.09 0.09 5.26 1.050448010414 FCA US LLC - Toledo North Assembly (0448010414) B012 290346.00 4619298.00 4.47 89.38 Yes 0.11 0.11 6.58 1.320448010414 FCA US LLC - Toledo North Assembly (0448010414) B013 290346.00 4619298.00 4.47 89.38 Yes 0.11 0.11 6.58 1.320448010414 FCA US LLC - Toledo North Assembly (0448010414) B014 290346.00 4619298.00 4.47 89.38 Yes 0.09 0.09 5.26 1.050448010414 FCA US LLC - Toledo North Assembly (0448010414) B015 290346.00 4619298.00 4.47 89.38 Yes 0.11 0.11 6.58 1.320448010414 FCA US LLC - Toledo North Assembly (0448010414) B016 290346.00 4619298.00 4.47 89.38 Yes 0.09 0.09 5.26 1.050448010414 FCA US LLC - Toledo North Assembly (0448010414) B017 290346.00 4619298.00 4.47 89.38 Yes 0.09 0.09 5.26 1.050448010414 FCA US LLC - Toledo North Assembly (0448010414) B018 290346.00 4619298.00 4.47 89.38 Yes 0.10 0.10 5.93 2.370448010414 FCA US LLC - Toledo North Assembly (0448010414) B019 290346.00 4619298.00 4.47 89.38 Yes 0.09 0.09 5.26 1.050448010414 FCA US LLC - Toledo North Assembly (0448010414) B020 290346.00 4619298.00 4.47 89.38 Yes 0.08 0.08 4.61 0.920448010414 FCA US LLC - Toledo North Assembly (0448010414) B021 290346.00 4619298.00 4.47 89.38 Yes 0.10 0.10 5.93 1.190448010414 FCA US LLC - Toledo North Assembly (0448010414) B022 290346.00 4619298.00 4.47 89.38 Yes 0.08 0.08 4.61 0.920448010414 FCA US LLC - Toledo North Assembly (0448010414) B023 290346.00 4619298.00 4.47 89.38 Yes 0.11 0.11 6.58 1.320448010414 FCA US LLC - Toledo North Assembly (0448010414) B024 290346.00 4619298.00 4.47 89.38 Yes 0.11 0.11 6.58 1.320448010414 FCA US LLC - Toledo North Assembly (0448010414) B025 290346.00 4619298.00 4.47 89.38 Yes 0.11 0.11 6.58 1.320448010414 FCA US LLC - Toledo North Assembly (0448010414) B026 290346.00 4619298.00 4.47 89.38 Yes 0.10 0.10 5.93 1.190448010414 FCA US LLC - Toledo North Assembly (0448010414) B027 290346.00 4619298.00 4.47 89.38 Yes 0.10 0.10 5.93 1.190448010414 FCA US LLC - Toledo North Assembly (0448010414) B028 290346.00 4619298.00 4.47 89.38 Yes 0.09 0.09 5.26 1.050448010414 FCA US LLC - Toledo North Assembly (0448010414) B029 290346.00 4619298.00 4.47 89.38 Yes 0.12 0.12 7.24 1.450448010414 FCA US LLC - Toledo North Assembly (0448010414) B030 290346.00 4619298.00 4.47 89.38 Yes 0.08 0.08 4.83 0.970448010414 FCA US LLC - Toledo North Assembly (0448010414) B031 290346.00 4619298.00 4.47 89.38 Yes 0.09 0.09 5.26 1.050448010414 FCA US LLC - Toledo North Assembly (0448010414) B402 290346.00 4619298.00 4.47 89.38 Yes 0.83 0.83 35.48 34.600448010414 FCA US LLC - Toledo North Assembly (0448010414) K021 PE67 290346.00 4619298.00 4.47 89.38 Yes 1.15 1.15 2.29 1.900448010414 FCA US LLC - Toledo North Assembly (0448010414) K022 PE01 290346.00 4619298.00 4.47 89.38 Yes 1.37 1.37 18.31 15.200448010414 FCA US LLC - Toledo North Assembly (0448010414) K022 PE03 290346.00 4619298.00 4.47 89.38 Yes 0.05 0.05 0.55 0.450448010414 FCA US LLC - Toledo North Assembly (0448010414) K022 PE05 290346.00 4619298.00 4.47 89.38 Yes 0.09 0.09 0.55 0.450448010414 FCA US LLC - Toledo North Assembly (0448010414) K022 PE06 290346.00 4619298.00 4.47 89.38 Yes 0.05 0.05 0.55 0.450448010414 FCA US LLC - Toledo North Assembly (0448010414) K022 PE07 290346.00 4619298.00 4.47 89.38 Yes 0.05 0.05 0.55 0.450448010414 FCA US LLC - Toledo North Assembly (0448010414) K023 PE67 290346.00 4619298.00 4.47 89.38 Yes 3.80 3.80 22.08 18.310448010414 FCA US LLC - Toledo North Assembly (0448010414) P008 PE73 290346.00 4619298.00 4.47 89.38 Yes 0.39 0.04 5.26 4.360448010414 FCA US LLC - Toledo North Assembly (0448010414) P008 PE74 290346.00 4619298.00 4.47 89.38 Yes 2.10 0.39 0.40 0.330448010414 FCA US LLC - Toledo North Assembly (0448010414) K023 PE48 290346.00 4619298.00 4.47 89.38 Yes 0.76 0.76 0.66 0.550448010414 FCA US LLC - Toledo North Assembly (0448010414) K023 PE49 290346.00 4619298.00 4.47 89.38 Yes 0.76 0.76 0.66 0.550448010414 FCA US LLC - Toledo North Assembly (0448010414) K023 PE50 290346.00 4619298.00 4.47 89.38 Yes 0.76 0.76 0.66 0.550448010414 FCA US LLC - Toledo North Assembly (0448010414) K023 PE51 290346.00 4619298.00 4.47 89.38 Yes 0.76 0.76 0.66 0.550448010414 FCA US LLC - Toledo North Assembly (0448010414) K023 PE53 290346.00 4619298.00 4.47 89.38 Yes 0.76 0.76 0.66 0.550448010414 FCA US LLC - Toledo North Assembly (0448010414) K024 290346.00 4619298.00 4.47 89.38 Yes 2.41 2.41 0.00 0.000448010414 FCA US LLC - Toledo North Assembly (0448010414) K027 290346.00 4619298.00 4.47 89.38 Yes 2.76 2.76 0.00 0.000448010414 FCA US LLC - Toledo North Assembly (0448010414) K029 290346.00 4619298.00 4.47 89.38 Yes 2.41 2.41 0.00 0.000448010414 FCA US LLC - Toledo North Assembly (0448010414) K402 290346.00 4619298.00 4.47 89.38 Yes 7.01 7.01 0.00 0.000448010414 FCA US LLC - Toledo North Assembly (0448010414) K407 290346.00 4619298.00 4.47 89.38 Yes 2.41 2.41 0.00 0.000448010414 FCA US LLC - Toledo North Assembly (0448010414) P011 PE33 290346.00 4619298.00 4.47 89.38 Yes 2.45 2.10 0.00 0.000448010414 FCA US LLC - Toledo North Assembly (0448010414) P012 BE01 290346.00 4619298.00 4.47 89.38 Yes 0.35 2.45 0.00 0.000448010414 FCA US LLC - Toledo North Assembly (0448010414) P012 BE02 290346.00 4619298.00 4.47 89.38 Yes 0.35 0.35 0.00 0.000448010414 FCA US LLC - Toledo North Assembly (0448010414) P012 BE05 290346.00 4619298.00 4.47 89.38 Yes 0.35 0.35 0.00 0.000448010414 FCA US LLC - Toledo North Assembly (0448010414) P012 BE06 290346.00 4619298.00 4.47 89.38 Yes 0.35 0.35 0.00 0.000448010414 FCA US LLC - Toledo North Assembly (0448010414) P012 BE07 290346.00 4619298.00 4.47 89.38 Yes 0.35 0.35 0.00 0.000448010414 Total 4.47 89.38 40.17 39.85 231.68 140.34 N N N N NA NA NA NA Screen Screen Model Model No No Yes Yes0448011731 FCA US LLC- Wrangler Paint Facility (0448011731) B301 SV76-BLR 289907.00 4618807.00 4.53 90.64 Yes 0.08 0.08 0.30 0.700448011731 FCA US LLC- Wrangler Paint Facility (0448011731) B303 Paint Mix 289907.00 4618807.00 4.53 90.64 Yes 0.24 0.24 10.95 1.380448011731 FCA US LLC- Wrangler Paint Facility (0448011731) B305 FUG-B305 289708.82 4618629.05 4.61 92.25 Yes 2.72 2.72 1.29 0.670448011731 FCA US LLC- Wrangler Paint Facility (0448011731) B306 289708.82 4618629.05 4.61 92.25 Yes 2.72 2.72 1.29 0.670448011731 FCA US LLC- Wrangler Paint Facility (0448011731) B307 289708.82 4618629.05 4.61 92.25 Yes 2.72 2.72 1.29 0.670448011731 FCA US LLC- Wrangler Paint Facility (0448011731) B308 289708.82 4618629.05 4.61 92.25 Yes 2.72 2.72 1.29 0.670448011731 FCA US LLC- Wrangler Paint Facility (0448011731) B309 289708.82 4618629.05 4.61 92.25 Yes 2.72 2.72 1.29 0.670448011731 FCA US LLC- Wrangler Paint Facility (0448011731) B310 289708.82 4618629.05 4.61 92.25 Yes 2.72 2.72 1.29 0.670448011731 FCA US LLC- Wrangler Paint Facility (0448011731) K301 SV50-RTO 289907.00 4618807.00 4.53 90.64 Yes 2.72 2.72 1.29 1.260448011731 FCA US LLC- Wrangler Paint Facility (0448011731) K302 SV01-RPC 289907.00 4618807.00 4.53 90.64 Yes 2.72 2.72 1.29 1.260448011731 FCA US LLC- Wrangler Paint Facility (0448011731) K303 SV50-RTO 289907.00 4618807.00 4.53 90.64 Yes 2.72 2.72 1.95 1.900448011731 FCA US LLC- Wrangler Paint Facility (0448011731) K303 SV04-BC 289907.00 4618807.00 4.53 90.64 Yes 2.72 2.72 0.96 0.930448011731 FCA US LLC- Wrangler Paint Facility (0448011731) K303 SV07-BCOB 289907.00 4618807.00 4.53 90.64 Yes 2.72 2.72 0.47 0.460448011731 FCA US LLC- Wrangler Paint Facility (0448011731) K303 SV11-CCOB 289907.00 4618807.00 4.53 90.64 Yes 2.72 2.72 0.47 0.460448011731 Total 4.53 90.64 32.91 32.91 25.39 12.36 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0448011576 Hoffman Road Landfill (0448011576) F002 F002 291397.63 4620215.51 4.48 89.64 Yes 0.58 0.96 2.18 40.630448011576 Hoffman Road Landfill (0448011576) F002 Fugitive 291397.63 4620215.51 4.48 89.64 Yes 4.25 4.25 10.24 13.540448011576 Hoffman Road Landfill (0448011576) F001 F001 291397.63 4620215.51 4.48 89.64 Yes 21.60 21.60 0.00 0.000448011576 Hoffman Road Landfill (0448011576) F003 F003 291397.63 4620215.51 4.48 89.64 Yes 0.20 1.36 0.00 0.000448011576 Total 4.48 89.64 26.63 28.16 12.42 54.17 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0448010466 Crown Cork & Seal (0448010466) K004 36-I2 290618.46 4620453.84 5.12 102.44 Yes 0.40 0.40 8.80 0.390448010466 Crown Cork & Seal (0448010466) K005 36-I 290618.46 4620453.84 5.12 102.44 Yes 0.22 0.22 11.60 2.150448010466 Total 5.12 102.44 0.62 0.62 20.40 2.54 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0448010051 ST. VINCENT MERCY MEDICAL CENTER (0448010051) B004 Boiler stack 1 288221.52 4616049.03 5.54 110.70 No 6.92 6.92 51.90 28.50

Page 307: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx CO0448010051 ST. VINCENT MERCY MEDICAL CENTER (0448010051) B005 Boiler stack 1 288221.52 4616049.03 5.54 110.70 No 6.92 6.92 51.90 28.500448010051 Total 5.54 110.70 13.84 13.84 103.81 56.99 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0448010246 Toledo Refining Company, LLC. (0448010246) B006 B006 STACK 292157.69 4611093.13 5.54 110.74 Yes 5.69 5.69 21.31 17.900448010246 Toledo Refining Company, LLC. (0448010246) B008 B008 STACK 292157.69 4611093.13 5.54 110.74 Yes 5.69 5.69 20.31 17.060448010246 Toledo Refining Company, LLC. (0448010246) B009 B009 STACK 292157.69 4611093.13 5.54 110.74 Yes 5.69 5.69 22.51 18.910448010246 Toledo Refining Company, LLC. (0448010246) B010 B010 STACK 292157.69 4611093.13 5.54 110.74 Yes 10.07 10.07 127.61 38.280448010246 Toledo Refining Company, LLC. (0448010246) B014 B014 STACK 292157.69 4611093.13 5.54 110.74 Yes 5.52 5.52 11.04 5.570448010246 Toledo Refining Company, LLC. (0448010246) B015 B015 STACK 292157.69 4611093.13 5.54 110.74 Yes 5.52 5.52 11.04 5.860448010246 Toledo Refining Company, LLC. (0448010246) B016 B016 STACK 292157.69 4611093.13 5.54 110.74 Yes 6.66 6.66 13.32 9.510448010246 Toledo Refining Company, LLC. (0448010246) B017 B017 STACK 292157.69 4611093.13 5.54 110.74 Yes 3.68 3.68 10.27 8.630448010246 Toledo Refining Company, LLC. (0448010246) B018 B018 STACK 292157.69 4611093.13 5.54 110.74 Yes 9.46 9.46 18.92 30.120448010246 Toledo Refining Company, LLC. (0448010246) B019 B019 STACK 292157.69 4611093.13 5.54 110.74 Yes 6.13 6.13 22.78 19.130448010246 Toledo Refining Company, LLC. (0448010246) B021 B021 STACK 292157.69 4611093.13 5.54 110.74 Yes 2.45 2.45 4.91 2.890448010246 Toledo Refining Company, LLC. (0448010246) B022 B022 STACK 292157.69 4611093.13 5.54 110.74 Yes 11.04 11.04 22.08 45.450448010246 Toledo Refining Company, LLC. (0448010246) B026 B026 STACK 292157.69 4611093.13 5.54 110.74 Yes 7.01 7.01 14.97 12.570448010246 Toledo Refining Company, LLC. (0448010246) B027 B027 STACK 292157.69 4611093.13 5.54 110.74 Yes 6.22 6.22 17.01 14.290448010246 Toledo Refining Company, LLC. (0448010246) B028 B028 STACK 292157.69 4611093.13 5.54 110.74 Yes 2.37 2.37 5.92 4.970448010246 Toledo Refining Company, LLC. (0448010246) B029 B029 STACK 292157.69 4611093.13 5.54 110.74 Yes 5.43 5.43 10.91 9.170448010246 Toledo Refining Company, LLC. (0448010246) B030 B030 STACK 292157.69 4611093.13 5.54 110.74 Yes 7.62 7.62 29.11 24.450448010246 Toledo Refining Company, LLC. (0448010246) B031 B031 STACK 292157.69 4611093.13 5.54 110.74 Yes 7.62 7.62 29.11 24.450448010246 Toledo Refining Company, LLC. (0448010246) B032 B033 STACK 292157.69 4611093.13 5.54 110.74 Yes 10.51 10.51 115.19 34.560448010246 Toledo Refining Company, LLC. (0448010246) B033 B033 STACK 292157.69 4611093.13 5.54 110.74 Yes 19.01 19.01 203.95 61.180448010246 Toledo Refining Company, LLC. (0448010246) B034 B034 STACK 292157.69 4611093.13 5.54 110.74 Yes 5.61 5.61 22.32 18.750448010246 Toledo Refining Company, LLC. (0448010246) B035 B034 STACK 292157.69 4611093.13 5.54 110.74 Yes 3.68 3.68 12.67 10.650448010246 Toledo Refining Company, LLC. (0448010246) B048 B048 STACK 292157.69 4611093.13 5.54 110.74 Yes 3.77 3.77 11.53 9.660448010246 Toledo Refining Company, LLC. (0448010246) B050 B050 STACK 292157.69 4611093.13 5.54 110.74 Yes 1.49 1.49 35.74 9.810448010246 Toledo Refining Company, LLC. (0448010246) B051 B051 STACK 292157.69 4611093.13 5.54 110.74 Yes 8.15 8.15 131.40 90.180448010246 Toledo Refining Company, LLC. (0448010246) B053 B053 STACK 292157.69 4611093.13 5.54 110.74 Yes 8.50 8.50 18.26 37.580448010246 Toledo Refining Company, LLC. (0448010246) B054 B054 STACK 292157.69 4611093.13 5.54 110.74 Yes 4.64 4.64 9.99 20.540448010246 Toledo Refining Company, LLC. (0448010246) B055 B055 STACK 292157.69 4611093.13 5.54 110.74 Yes 1.36 1.36 7.01 14.410448010246 Toledo Refining Company, LLC. (0448010246) B056 B056 STACK 292157.69 4611093.13 5.54 110.74 Yes 1.64 1.64 8.79 18.090448010246 Toledo Refining Company, LLC. (0448010246) B057 B057 STACK 292157.69 4611093.13 5.54 110.74 Yes 1.54 1.54 8.29 17.070448010246 Toledo Refining Company, LLC. (0448010246) P008 P008 STACK 292157.69 4611093.13 5.54 110.74 Yes 3.67 3.67 28.29 147.310448010246 Toledo Refining Company, LLC. (0448010246) P009 P009 STACK 292157.69 4611093.13 5.54 110.74 Yes 69.51 69.51 15.09 77.010448010246 Toledo Refining Company, LLC. (0448010246) P011 WGS Stack 292157.69 4611093.13 5.54 110.74 Yes 331.92 331.92 198.41 272.150448010246 Toledo Refining Company, LLC. (0448010246) P012 P012 STACK 292157.69 4611093.13 5.54 110.74 Yes 2.45 2.45 3.30 6.600448010246 Toledo Refining Company, LLC. (0448010246) P035 P035-STACK 292157.69 4611093.13 5.54 110.74 Yes 0.37 0.37 51.76 7.270448010246 Toledo Refining Company, LLC. (0448010246) P036 P036-STACK 292157.69 4611093.13 5.54 110.74 Yes 0.37 0.37 51.76 7.270448010246 Toledo Refining Company, LLC. (0448010246) P041 P041 STACK 292157.69 4611093.13 5.54 110.74 Yes 5.96 5.96 11.17 22.380448010246 Toledo Refining Company, LLC. (0448010246) F001 F001 FUG 292157.69 4611093.13 5.54 110.74 Yes 0.31 1.78 0.00 0.000448010246 Toledo Refining Company, LLC. (0448010246) P042 Z011FUG -Cooling Tower 292157.69 4611093.13 5.54 110.74 Yes 4.76 23.80 0.00 0.000448010246 Toledo Refining Company, LLC. (0448010246) P043 Z012FUG - Cooling Tower 292157.69 4611093.13 5.54 110.74 Yes 0.89 4.45 0.00 0.000448010246 Toledo Refining Company, LLC. (0448010246) P044 Z013FUG - Cooling Tower 292157.69 4611093.13 5.54 110.74 Yes 11.79 58.95 0.00 0.000448010246 Toledo Refining Company, LLC. (0448010246) P045 Z014FUG - Cooling Tower 292157.69 4611093.13 5.54 110.74 Yes 10.60 53.00 0.00 0.000448010246 Toledo Refining Company, LLC. (0448010246) P046 Z015FUG - Cooling Tower 292157.69 4611093.13 5.54 110.74 Yes 7.16 35.80 0.00 0.000448010246 Toledo Refining Company, LLC. (0448010246) B022 B022 STACK 292157.69 4611093.13 5.54 110.74 Yes 11.04 11.04 22.08 0.000448010246 Toledo Refining Company, LLC. (0448010246) B052 B052 STACK 292157.69 4611093.13 5.54 110.74 Yes 0.65 0.65 1.30 0.000448010246 Toledo Refining Company, LLC. (0448010246) P040 CoolingTower 292157.69 4611093.13 5.54 110.74 Yes 0.53 0.53 0.00 0.000448010246 Total 5.54 110.74 645.72 787.99 1381.39 1191.70 N N N N NA NA NA NA Model Model Model Model Yes Yes Yes Yes0448010133 Perstorp Polyols, Inc. (0448010133) P812 Fugitive emissions from Formox mfg 289496.65 4620054.43 5.61 112.12 Yes 0.00 0.00 0.00 0.030448010133 Perstorp Polyols, Inc. (0448010133) P803 Fugitive emissions from Penta Mfg. 289496.65 4620054.43 5.61 112.12 Yes 0.00 0.00 0.00 0.000448010133 Perstorp Polyols, Inc. (0448010133) B001 B-001 289343.00 4619943.00 5.65 113.05 Yes 7.45 7.45 36.50 35.780448010133 Perstorp Polyols, Inc. (0448010133) P812 Vent #2 289343.00 4619943.00 5.65 113.05 Yes 0.00 0.00 0.00 13.710448010133 Perstorp Polyols, Inc. (0448010133) P803 T-200 289343.00 4619943.00 5.65 113.05 Yes 2.46 2.46 0.00 0.000448010133 Perstorp Polyols, Inc. (0448010133) P803 T-290 289343.00 4619943.00 5.65 113.05 Yes 2.46 2.46 0.00 0.000448010133 Perstorp Polyols, Inc. (0448010133) P803 T-316 289343.00 4619943.00 5.65 113.05 Yes 2.46 2.46 0.00 0.000448010133 Perstorp Polyols, Inc. (0448010133) P803 T-350 289343.00 4619943.00 5.65 113.05 Yes 2.46 2.46 0.00 0.000448010133 Total 5.65 113.05 17.30 17.30 36.50 49.52 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0448011196 THE ANDERSONS, INC. (0448011196) F004 288608.34 4611924.64 6.81 136.24 No 0.05 0.28 0.72 0.120448011196 THE ANDERSONS, INC. (0448011196) F005 288608.34 4611924.64 6.81 136.24 No 0.07 0.43 1.09 0.180448011196 THE ANDERSONS, INC. (0448011196) F001 288608.34 4611924.64 6.81 136.24 No 0.00 0.32 0.00 0.000448011196 THE ANDERSONS, INC. (0448011196) F003 288608.34 4611924.64 6.81 136.24 No 0.03 0.16 0.00 0.000448011196 THE ANDERSONS, INC. (0448011196) P901 288608.34 4611924.64 6.81 136.24 No 0.03 0.14 0.00 0.000448011196 THE ANDERSONS, INC. (0448011196) P902 288608.34 4611924.64 6.81 136.24 No 0.00 0.01 0.00 0.000448011196 THE ANDERSONS, INC. (0448011196) P905 288608.34 4611924.64 6.81 136.24 No 0.05 0.29 0.00 0.000448011196 Total 6.81 136.24 100.00 100.00 100.00 100.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0448011189 OmniSource Corporation (0448011189) F001 288470.22 4620548.11 6.71 134.25 No 0.00 8.17 0.00 0.000448011189 OmniSource Corporation (0448011189) F002 Material Storage Piles 288470.22 4620548.11 6.71 134.25 No 0.00 6.93 0.00 0.000448011189 OmniSource Corporation (0448011189) F003 288470.22 4620548.11 6.71 134.25 No 0.00 2.66 0.00 0.000448011189 OmniSource Corporation (0448011189) F005 Shredder Feed Chute Entrance 288470.22 4620548.11 6.71 134.25 No 0.00 0.07 0.00 0.000448011189 Total 6.71 134.25 100.00 100.00 100.00 100.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0448011937 TRANSFLO Terminal Services, Inc. (0448011937) P901 baghouse exhaust 289109.24 4611009.76 7.11 142.16 No 38.41 38.41 0.00 0.000448011937 TRANSFLO Terminal Services, Inc. (0448011937) P901 289109.24 4611009.76 7.11 142.16 No 0.00 0.00 0.00 0.000448011937 Total 7.11 142.16 38.41 38.41 0.00 0.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0448010300 NORTH TOLEDO GRAPHICS LLC (0448010300) K002 RTO Stack #1 288040.96 4620900.87 7.27 145.36 No 0.29 0.29 7.14 6.090448010300 NORTH TOLEDO GRAPHICS LLC (0448010300) K002 Bypass Stack 288040.96 4620900.87 7.27 145.36 No 0.00 0.00 0.87 0.730448010300 NORTH TOLEDO GRAPHICS LLC (0448010300) K005 RTO Stack #1 288040.96 4620900.87 7.27 145.36 No 0.00 0.00 0.60 0.52

Page 308: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx CO0448010300 NORTH TOLEDO GRAPHICS LLC (0448010300) K005 Bypass Stack 288040.96 4620900.87 7.27 145.36 No 0.00 0.00 0.62 0.540448010300 NORTH TOLEDO GRAPHICS LLC (0448010300) K007 RTO Stack #1 288040.96 4620900.87 7.27 145.36 No 0.00 0.00 0.79 0.660448010300 NORTH TOLEDO GRAPHICS LLC (0448010300) K007 Bypass Stack 288040.96 4620900.87 7.27 145.36 No 0.00 0.00 0.83 0.690448010300 NORTH TOLEDO GRAPHICS LLC (0448010300) K009 Bypass Stack 288040.96 4620900.87 7.27 145.36 No 0.00 0.00 0.41 0.350448010300 NORTH TOLEDO GRAPHICS LLC (0448010300) K009 M1000 RT Stack 288040.96 4620900.87 7.27 145.36 No 0.00 0.00 0.40 0.340448010300 NORTH TOLEDO GRAPHICS LLC (0448010300) K002 Roof Fans 288040.96 4620900.87 7.27 145.36 No 0.00 0.00 0.03 0.030448010300 NORTH TOLEDO GRAPHICS LLC (0448010300) K005 Roof Fans 288040.96 4620900.87 7.27 145.36 No 0.00 0.00 0.02 0.020448010300 NORTH TOLEDO GRAPHICS LLC (0448010300) K007 Roof Fans 288040.96 4620900.87 7.27 145.36 No 0.00 0.00 0.03 0.030448010300 NORTH TOLEDO GRAPHICS LLC (0448010300) K009 Roof Fans 288040.96 4620900.87 7.27 145.36 No 0.00 0.00 0.01 0.010448010300 Total 7.27 145.36 100.00 100.00 100.00 100.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0387000259 Evergreen Recycling and Disposal Facility (0387000259) P901 Open Flare 292522.11 4608668.92 7.83 156.50 Yes 10.77 10.77 43.06 234.330387000259 Evergreen Recycling and Disposal Facility (0387000259) F005 F005 292522.11 4608668.92 7.83 156.50 Yes 9.75 195.00 0.00 0.000387000259 Evergreen Recycling and Disposal Facility (0387000259) P901 P901 292522.11 4608668.92 7.83 156.50 Yes 0.02 1.77 6.63 36.050387000259 Evergreen Recycling and Disposal Facility (0387000259) P901 F005 292522.11 4608668.92 7.83 156.50 Yes 0.02 1.77 6.63 36.050387000259 Total 7.83 156.50 20.56 209.30 56.31 306.43 N N N N NA NA NA NA Screen Model Screen Model No Yes No Yes0448010370 Tembec BTLSR Inc (0448010370) B001 Boilers 1 & 2 Stack - Common 285785.00 4615442.00 8.02 160.36 Yes 14.66 14.66 3.59 3.020448010370 Tembec BTLSR Inc (0448010370) B002 Boilers 1 & 2 Stack - Common 285785.00 4615442.00 8.02 160.36 Yes 0.03 0.05 0.41 0.350448010370 Tembec BTLSR Inc (0448010370) P001 A System Stack 285785.00 4615442.00 8.02 160.36 Yes 16.64 16.64 0.44 0.370448010370 Tembec BTLSR Inc (0448010370) P002 B System Stack 285785.00 4615442.00 8.02 160.36 Yes 16.64 16.64 0.68 0.570448010370 Tembec BTLSR Inc (0448010370) P003 C System Stack 285785.00 4615442.00 8.02 160.36 Yes 16.64 16.64 0.68 100.500448010370 Tembec BTLSR Inc (0448010370) P012 285785.00 4615442.00 8.02 160.36 Yes 16.64 16.64 0.00 0.000448010370 Tembec BTLSR Inc (0448010370) P013 Backup Electrical Generator Emissions 285785.00 4615442.00 8.02 160.36 Yes 0.00 0.00 0.00 0.000448010370 Total 8.02 160.36 81.27 81.29 5.81 104.81 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0387000046 MSC Walbridge Coatings Inc (0387000046) B001 epsB001 290892.00 4608407.21 8.48 169.70 Yes 1.80 1.80 10.69 8.980387000046 MSC Walbridge Coatings Inc (0387000046) B002 epsB002 290892.00 4608407.21 8.48 169.70 Yes 0.05 0.05 3.07 2.630387000046 MSC Walbridge Coatings Inc (0387000046) B003 epsB003 290892.00 4608407.21 8.48 169.70 Yes 1.80 1.80 10.69 8.980387000046 MSC Walbridge Coatings Inc (0387000046) K001 epsK001 290892.00 4608407.21 8.48 169.70 Yes 1.06 1.06 55.82 46.890387000046 MSC Walbridge Coatings Inc (0387000046) K002 epsK001 290892.00 4608407.21 8.48 169.70 Yes 0.15 0.15 2.45 2.060387000046 MSC Walbridge Coatings Inc (0387000046) P001 epsP001 290892.00 4608407.21 8.48 169.70 Yes 6.53 6.53 0.00 0.000387000046 Total 8.48 169.70 11.38 11.38 82.72 69.54 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoN2689 VIENNA JUNCTION LANDFILL 1 Enclosed Flare 291000.00 4625000.00 9.03 180.60 No 0.00 0.00 4.51 15.03N2689 BROWNING-FERRIS INDUSTRIES 2 LANDFILL GAS FLARE 291000.00 4625000.00 9.03 180.60 No 0.00 0.00 4.51 147.61N2689 VIENNA JUNCTION LANDFILL 3 291000.00 4625000.00 9.03 180.60 No 87.32 87.32 4.51 15.03N2689 Total 9.03 180.60 100.00 100.00 100.00 100.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0387040084 BOWERS ASPHALT & PAVING, INC (0387040084) P003 Electric Generator Exhaust 290422.06 4607017.37 9.95 199.03 No 0.59 0.59 30.27 2.410387040084 BOWERS ASPHALT & PAVING, INC (0387040084) P901 Baghouse Stack 290422.06 4607017.37 9.95 199.03 No 29.43 29.43 84.10 280.320387040084 BOWERS ASPHALT & PAVING, INC (0387040084) P901 290422.06 4607017.37 9.95 199.03 No 1.64 1.64 0.05 0.230387040084 Total 9.95 199.03 100.00 100.00 100.00 100.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0487010012 Pilkington North America Inc (0487010012) B021 B021 286571.12 4609416.64 10.01 200.21 Yes 0.11 0.14 1.90 1.600487010012 Pilkington North America Inc (0487010012) B022 B022 286571.12 4609416.64 10.01 200.21 Yes 0.08 0.11 1.44 1.210487010012 Pilkington North America Inc (0487010012) B023 B023 286571.12 4609416.64 10.01 200.21 Yes 0.08 0.11 1.44 1.210487010012 Pilkington North America Inc (0487010012) P001 6F1 Ejct. N 286571.12 4609416.64 10.01 200.21 Yes 27.34 28.70 57.61 0.140487010012 Pilkington North America Inc (0487010012) P001 6F1 Ejct. S 286571.12 4609416.64 10.01 200.21 Yes 27.34 28.70 57.61 0.140487010012 Pilkington North America Inc (0487010012) P001 6F1 Stack 286571.12 4609416.64 10.01 200.21 Yes 170.38 170.38 364.72 16.990487010012 Pilkington North America Inc (0487010012) P003 6F3 Stack 286571.12 4609416.64 10.01 200.21 Yes 179.58 179.58 963.60 876.000487010012 Pilkington North America Inc (0487010012) F007 Feed Rec Transfer System 286571.12 4609416.64 10.01 200.21 Yes 1.31 174.32 0.00 0.000487010012 Pilkington North America Inc (0487010012) F008 Batch and Cullet Feed System 286571.12 4609416.64 10.01 200.21 Yes 1.93 1.93 0.00 0.000487010012 Pilkington North America Inc (0487010012) F003 6F1 Hot End Cullet Handling System 286571.12 4609416.64 10.01 200.21 Yes 3.82 39.81 0.00 0.000487010012 Pilkington North America Inc (0487010012) F004 6F1 Cold End Cullet Handling System 286571.12 4609416.64 10.01 200.21 Yes 16.57 102.62 0.00 0.000487010012 Pilkington North America Inc (0487010012) F005 6F3 Hot End Cullet Handling System 286571.12 4609416.64 10.01 200.21 Yes 3.82 45.99 0.00 0.000487010012 Pilkington North America Inc (0487010012) F006 6F3 Cold End Cullet Handling System 286571.12 4609416.64 10.01 200.21 Yes 14.80 118.70 0.00 0.000487010012 Pilkington North America Inc (0487010012) P012 Emer Engine 286571.12 4609416.64 10.01 200.21 Yes 4.38 4.38 43.80 13.580487010012 Pilkington North America Inc (0487010012) P013 Emer Engine 286571.12 4609416.64 10.01 200.21 Yes 4.38 4.38 43.80 13.580487010012 Pilkington North America Inc (0487010012) P014 Emer Engine 286571.12 4609416.64 10.01 200.21 Yes 4.38 4.38 43.80 13.580487010012 Total 10.01 200.21 460.20 904.10 1577.83 936.42 N N N N NA NA NA NA Model Model Model Model Yes Yes Yes Yes0448010404 General Motors LLC - Toledo (0448010404) B001 Boiler 1 Stack 285507.31 4622025.46 9.98 199.54 Yes 6.13 6.13 15.03 25.250448010404 General Motors LLC - Toledo (0448010404) B003 Boiler #3 Stack 285507.31 4622025.46 9.98 199.54 Yes 6.61 6.61 16.21 27.230448010404 General Motors LLC - Toledo (0448010404) B004 Boiler #4 Stack 285507.31 4622025.46 9.98 199.54 Yes 6.61 6.61 16.21 27.230448010404 Total 9.98 199.54 19.36 19.36 47.45 79.72 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0387000362 Norplas Industries Inc. (0387000362) R001 1 Bake Z1 287960.55 4607998.59 10.20 203.97 Yes 0.10 0.41 3.77 3.150387000362 Norplas Industries Inc. (0387000362) B001 HWG-B001 287960.55 4607998.59 10.20 203.97 Yes 0.07 0.07 0.91 0.760387000362 Norplas Industries Inc. (0387000362) R001 1 Bake Z2 287960.55 4607998.59 10.20 203.97 Yes 0.10 0.41 0.94 1.050387000362 Norplas Industries Inc. (0387000362) R001 1 Bake Z3 287960.55 4607998.59 10.20 203.97 Yes 0.10 0.41 0.94 1.050387000362 Norplas Industries Inc. (0387000362) R001 1 Dry Off 287960.55 4607998.59 10.20 203.97 Yes 0.10 0.41 0.94 1.050387000362 Norplas Industries Inc. (0387000362) R001 1 B/C EMS 287960.55 4607998.59 10.20 203.97 Yes 0.05 0.23 0.52 0.580387000362 Norplas Industries Inc. (0387000362) R001 1A/P EMS 287960.55 4607998.59 10.20 203.97 Yes 0.02 0.08 0.19 0.210387000362 Norplas Industries Inc. (0387000362) R001 RTO 287960.55 4607998.59 10.20 203.97 Yes 4.38 4.38 8.76 13.580387000362 Norplas Industries Inc. (0387000362) R001 Spraymation Booth Emergency Exhaust 287960.55 4607998.59 10.20 203.97 Yes 0.10 0.43 0.99 1.110387000362 Norplas Industries Inc. (0387000362) R001 Paint Sludge Pit Fugitive Emissions 287960.55 4607998.59 10.20 203.97 Yes 0.26 1.14 2.59 2.900387000362 Total 10.20 203.97 5.26 7.98 20.55 25.45 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0448010386 SHELLY MATERIALS PLANT # 4132 (0448010386) P901 Hot Mix Asphalt Stack 283209.00 4614406.00 10.72 214.47 No 59.79 59.79 110.38 367.920448010386 SHELLY MATERIALS PLANT # 4132 (0448010386) P901 FAGGS-P901 283209.00 4614406.00 10.72 214.47 No 0.00 0.00 1.00 6.500448010386 Total 10.72 214.47 100.00 100.00 100.00 100.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0387000107 American Warming and Ventilating, a division of Mestek (0387000107) K001 Flash-off Area Stack 4 298550.42 4606336.13 11.15 223.00 No 0.01 0.16 0.23 0.200387000107 American Warming and Ventilating, a division of Mestek (0387000107) K001 Drying Oven - Stack 5 298550.42 4606336.13 11.15 223.00 No 0.01 0.16 0.23 0.200387000107 American Warming and Ventilating, a division of Mestek (0387000107) K001 Primer Booth #2 Stack 298550.42 4606336.13 11.15 223.00 No 0.01 0.15 0.22 0.180387000107 American Warming and Ventilating, a division of Mestek (0387000107) K001 Primer Booth #1 Stack 298550.42 4606336.13 11.15 223.00 No 0.01 0.15 0.22 0.18

Page 309: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx CO0387000107 American Warming and Ventilating, a division of Mestek (0387000107) K001 Paint Booth 1 Stack 298550.42 4606336.13 11.15 223.00 No 0.01 0.07 0.11 0.090387000107 American Warming and Ventilating, a division of Mestek (0387000107) K001 Paint Booth 2 Stack 298550.42 4606336.13 11.15 223.00 No 0.01 0.07 0.11 0.090387000107 American Warming and Ventilating, a division of Mestek (0387000107) K001 Flash-off Area Stack 3 298550.42 4606336.13 11.15 223.00 No 0.01 0.07 0.11 0.090387000107 American Warming and Ventilating, a division of Mestek (0387000107) K001 Flash-off Area Stack 2 298550.42 4606336.13 11.15 223.00 No 0.01 0.08 0.11 0.090387000107 American Warming and Ventilating, a division of Mestek (0387000107) K001 Fugitive Emissions from Cleanup Operations 298550.42 4606336.13 11.15 223.00 No 0.00 0.02 0.03 0.020387000107 Total 11.15 223.00 100.00 100.00 100.00 100.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0387040334 Calphalon Group, Newell - Rubbermaid, Inc. (0387040334) K003 Main Cure Oven - Cooling Chamber Exhaust 288017.61 4606623.33 11.33 226.58 No 0.00 0.01 0.38 0.320387040334 Calphalon Group, Newell - Rubbermaid, Inc. (0387040334) K003 Main Cure Oven - Burner Box Exhaust 288017.61 4606623.33 11.33 226.58 No 0.00 0.01 0.39 0.330387040334 Calphalon Group, Newell - Rubbermaid, Inc. (0387040334) K003 Main Cure Oven - Infeed Fume Hood 288017.61 4606623.33 11.33 226.58 No 0.00 0.01 0.38 0.320387040334 Calphalon Group, Newell - Rubbermaid, Inc. (0387040334) K004 Main Cure Oven - Cooling Chamber Exhaust 288017.61 4606623.33 11.33 226.58 No 0.00 0.01 0.38 0.320387040334 Calphalon Group, Newell - Rubbermaid, Inc. (0387040334) K004 Main Cure Oven - Burner Box Exhaust 288017.61 4606623.33 11.33 226.58 No 0.00 0.01 0.39 0.330387040334 Calphalon Group, Newell - Rubbermaid, Inc. (0387040334) K004 Main Cure Oven - Infeed Fume Hood 288017.61 4606623.33 11.33 226.58 No 0.00 0.01 0.38 0.320387040334 Total 11.33 226.58 100.00 100.00 100.00 100.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0448010805 UNIVERSITY OF TOLEDO - MAIN CAMPUS (0448010805) B018 Common Stack for Student Recreation Center Boi 282369.20 4615420.75 11.42 228.37 No 0.00 0.00 0.00 0.000448010805 UNIVERSITY OF TOLEDO - MAIN CAMPUS (0448010805) B020 Stack for Steam Generator Nos. 1 thru 8 282369.20 4615420.75 11.42 228.37 No 0.00 0.00 0.00 0.000448010805 UNIVERSITY OF TOLEDO - MAIN CAMPUS (0448010805) B021 Stack for Steam Generator Nos. 1 thru 8 282369.20 4615420.75 11.42 228.37 No 0.00 0.00 0.00 0.000448010805 UNIVERSITY OF TOLEDO - MAIN CAMPUS (0448010805) B022 Stack for Steam Generator Nos. 1 thru 8 282369.20 4615420.75 11.42 228.37 No 0.00 0.00 0.00 0.000448010805 UNIVERSITY OF TOLEDO - MAIN CAMPUS (0448010805) B024 Stack for Steam Generator Nos. 1 thru 8 282369.20 4615420.75 11.42 228.37 No 0.00 0.00 0.00 0.000448010805 UNIVERSITY OF TOLEDO - MAIN CAMPUS (0448010805) B025 Stack for Steam Generator Nos. 1 thru 8 282369.20 4615420.75 11.42 228.37 No 0.00 0.00 0.00 0.000448010805 UNIVERSITY OF TOLEDO - MAIN CAMPUS (0448010805) B026 Stack for Steam Generator Nos. 1 thru 8 282369.20 4615420.75 11.42 228.37 No 0.00 0.00 0.00 0.000448010805 UNIVERSITY OF TOLEDO - MAIN CAMPUS (0448010805) B027 Stack for Steam Generator Nos. 1 thru 8 282369.20 4615420.75 11.42 228.37 No 0.00 0.00 0.00 0.000448010805 UNIVERSITY OF TOLEDO - MAIN CAMPUS (0448010805) B028 Stack for Steam Generator Nos. 1 thru 8 282369.20 4615420.75 11.42 228.37 No 0.00 0.00 0.00 0.000448010805 Total 11.42 228.37 100.00 100.00 100.00 100.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0448011193 Decorative Panels International Inc (0448011193) K001 S16 282413.86 4613073.27 11.81 236.19 Yes 0.00 0.00 1.27 0.000448011193 Decorative Panels International Inc (0448011193) K001 S17 282413.86 4613073.27 11.81 236.19 Yes 0.00 0.00 1.27 0.000448011193 Decorative Panels International Inc (0448011193) K001 S18 282413.86 4613073.27 11.81 236.19 Yes 0.00 0.00 1.21 0.000448011193 Decorative Panels International Inc (0448011193) K001 S22 282413.86 4613073.27 11.81 236.19 Yes 0.00 0.00 1.21 0.000448011193 Decorative Panels International Inc (0448011193) K001 282413.86 4613073.27 11.81 236.19 Yes 0.00 0.00 0.81 0.000448011193 Total 11.81 236.19 0.00 0.00 5.75 0.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoF5756 R J MARSHALL COMPANY HAMMERMILL WITH DUST COLLECTOR 291780.00 4628840.00 12.60 251.93 0.00 3.94 0.00 0.00F5756 R J MARSHALL COMPANY GRINDER/CLASSIFIER 291780.00 4628840.00 12.60 251.93 0.00 3.71 0.00 0.00F5756 Total 12.60 251.93 0.00 7.65 0.00 0.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0448010247 University of Toledo Health Science Campus (0448010247) B008 FSB Steam Generator No. 1 Stack 282093.37 4610891.36 12.89 257.76 No 0.17 0.17 2.18 1.830448010247 University of Toledo Health Science Campus (0448010247) B009 FSB Steam Generator No. 2 Stack 282093.37 4610891.36 12.89 257.76 No 0.17 0.17 2.18 1.830448010247 University of Toledo Health Science Campus (0448010247) B010 FSB Steam Generator No. 3 Stack 282093.37 4610891.36 12.89 257.76 No 0.17 0.17 2.18 1.830448010247 University of Toledo Health Science Campus (0448010247) B011 FSB Steam Generator No. 4 Stack 282093.37 4610891.36 12.89 257.76 No 0.17 0.17 2.18 1.830448010247 University of Toledo Health Science Campus (0448010247) B013 FSB Boiler #5 Stack 282093.37 4610891.36 12.89 257.76 No 0.17 0.17 2.18 1.830448010247 University of Toledo Health Science Campus (0448010247) B014 FSB Boiler #6 Stack 282093.37 4610891.36 12.89 257.76 No 0.17 0.17 2.18 1.830448010247 University of Toledo Health Science Campus (0448010247) P007 Exhaust Pipe FSB Emergency Generator 282093.37 4610891.36 12.89 257.76 No 0.00 0.00 0.11 0.020448010247 University of Toledo Health Science Campus (0448010247) P101 S/P101 282093.37 4610891.36 12.89 257.76 No 0.02 0.02 0.22 0.050448010247 University of Toledo Health Science Campus (0448010247) P102 S/P102 282093.37 4610891.36 12.89 257.76 No 0.01 0.01 0.21 0.040448010247 University of Toledo Health Science Campus (0448010247) P105 A/P105 282093.37 4610891.36 12.89 257.76 No 0.01 0.01 0.19 0.040448010247 University of Toledo Health Science Campus (0448010247) P106 Exhaust Pipe Dowling Emergency Generator #3 282093.37 4610891.36 12.89 257.76 No 0.00 0.00 0.19 0.040448010247 Total 12.89 257.76 100.00 100.00 100.00 100.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoB2846 J.R. WHITING CO 1 Breaker house dust exhauster. 296440.00 4629490.00 13.37 267.33 0.00 3.59 0.00 0.00B2846 J.R. WHITING CO 2 Upgraded Dust Collector replaces SVBunker1, SVB 296440.00 4629490.00 13.37 267.33 0.00 3.59 0.00 0.00B2846 J.R. WHITING CO 3 Serves the rail car coal unloading facility 296440.00 4629490.00 13.37 267.33 0.00 3.59 0.00 0.00B2846 J.R. WHITING CO 4 Serves the coal conveyor room 296440.00 4629490.00 13.37 267.33 0.00 3.59 0.00 0.00B2846 J.R. WHITING CO 5 Fly ash system secondary collector. 296440.00 4629490.00 13.37 267.33 0.00 11.37 0.00 0.00B2846 J.R. WHITING CO 6 Silo baghouse vent. 296440.00 4629490.00 13.37 267.33 0.00 5.68 0.00 0.00B2846 J.R. WHITING CO 7 Fly ash system hydroveyor. 296440.00 4629490.00 13.37 267.33 0.00 5.68 0.00 0.00B2846 J.R. WHITING CO 8 Boiler #2 stack. 296440.00 4629490.00 13.37 267.33 0.00 111.74 821.79 87.93B2846 J.R. WHITING CO 9 Boiler #1 stack. 296440.00 4629490.00 13.37 267.33 0.00 342.60 801.02 94.09B2846 J.R. WHITING CO 10 Boiler #3 stack. 296440.00 4629490.00 13.37 267.33 0.00 516.06 947.70 117.22B2846 CONSUMERS ENERGY COMPANY 11 ELEC UTILITY STEAM GENRATINGUNIT 296440.00 4629490.00 13.37 267.33 0.00 3679.20 0.00 400.00B2846 CONSUMERS ENERGY COMPANY 12 COAL HANDLING EQUIPMENT 296440.00 4629490.00 13.37 267.33 0.00 37.16 0.00 0.00B2846 J.R. WHITING CO 296440.00 4629490.00 13.37 267.33 0.58 3.59 32.64 5.25B2846 Total 13.37 267.33 0.58 4727.46 2603.15 704.49 N N N N NA NA NA NA Screen Model Model Model No Yes Yes Yes0387040123 FCA US LLC - Toledo Machining Plant (0387040123) B015 B015 288386.79 4603571.95 13.90 278.01 No 0.42 0.42 4.81 0.470387040123 FCA US LLC - Toledo Machining Plant (0387040123) B018 288386.79 4603571.95 13.90 278.01 No 0.15 0.15 1.75 0.170387040123 FCA US LLC - Toledo Machining Plant (0387040123) P018 Fugitive emissions from each of 20 wire welders 288386.79 4603571.95 13.90 278.01 No 0.00 3.32 0.00 0.000387040123 Total 13.90 278.01 100.00 100.00 100.00 100.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0448011215 HA INTERNATIONAL LLC (0448011215) P002 Micropul dust collector exhaust (serves solvent ro 280600.63 4610565.60 14.38 287.62 No 0.02 0.04 0.00 0.000448011215 HA INTERNATIONAL LLC (0448011215) P005 Micropul dust collector exhaust (serves solvent ro 280600.63 4610565.60 14.38 287.62 No 0.01 0.02 0.00 0.000448011215 HA INTERNATIONAL LLC (0448011215) P011 Micropul dust collector exhaust (serves solvent ro 280600.63 4610565.60 14.38 287.62 No 0.00 0.00 0.00 0.000448011215 HA INTERNATIONAL LLC (0448011215) P018 Sly Baghouse Exhaust (serves water-based produc 280600.63 4610565.60 14.38 287.62 No 0.07 0.12 0.00 0.000448011215 HA INTERNATIONAL LLC (0448011215) P021 Sly Baghouse Exhaust (serves water-based produc 280600.63 4610565.60 14.38 287.62 No 0.05 0.07 0.00 0.000448011215 HA INTERNATIONAL LLC (0448011215) P022 Sly Baghouse Exhaust (serves water-based produc 280600.63 4610565.60 14.38 287.62 No 0.35 0.60 0.00 0.000448011215 HA INTERNATIONAL LLC (0448011215) P023 Sly Baghouse Exhaust (serves water-based produc 280600.63 4610565.60 14.38 287.62 No 0.07 0.16 0.00 0.000448011215 HA INTERNATIONAL LLC (0448011215) P028 Torit Exhaust Stack 280600.63 4610565.60 14.38 287.62 No 0.01 0.01 0.00 0.000448011215 HA INTERNATIONAL LLC (0448011215) P002 280600.63 4610565.60 14.38 287.62 No 0.01 0.01 0.00 0.000448011215 HA INTERNATIONAL LLC (0448011215) P005 280600.63 4610565.60 14.38 287.62 No 0.00 0.01 0.00 0.000448011215 HA INTERNATIONAL LLC (0448011215) P011 280600.63 4610565.60 14.38 287.62 No 0.00 0.00 0.00 0.000448011215 HA INTERNATIONAL LLC (0448011215) P018 280600.63 4610565.60 14.38 287.62 No 0.02 0.03 0.00 0.000448011215 HA INTERNATIONAL LLC (0448011215) P021 280600.63 4610565.60 14.38 287.62 No 0.01 0.02 0.00 0.000448011215 HA INTERNATIONAL LLC (0448011215) P022 280600.63 4610565.60 14.38 287.62 No 0.10 0.18 0.00 0.000448011215 HA INTERNATIONAL LLC (0448011215) P023 280600.63 4610565.60 14.38 287.62 No 0.02 0.05 0.00 0.00

Page 310: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx CO0448011215 HA INTERNATIONAL LLC (0448011215) P028 280600.63 4610565.60 14.38 287.62 No 0.00 0.00 0.00 0.000448011215 Total 14.38 287.62 100.00 100.00 100.00 100.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoB4922 STONECO, INC 1 A combination of process equipment (screens, cru 278652.00 4625040.00 17.39 347.86 No 0.00 0.00 0.00 0.00B4922 STONECO INC 2 278652.00 4625040.00 17.39 347.86 No 30.18 30.18 0.00 0.00B4922 Total 17.39 347.86 100.00 100.00 100.00 100.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoN1536 GERKEN MATERIALS, INC asphalt plant baghouse stack 278300.00 4625040.00 17.70 353.98 No 0.00 0.00 0.00 0.00N1536 Total 17.70 353.98 100.00 100.00 100.00 100.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No

448030014 Stoneco Plant # 110 (0448030014) P931 P931 Baghouse Stack 277419.55 4605847.70 19.44 388.77 No 0.00 0.00 213.53 159.43448030014 Total 19.44 388.77 0.00 0.00 213.53 159.43 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0448031076 The Andersons, Inc. (0448031076) K001 Paint Booth Stack 277764.15 4605250.22 19.49 389.71 No 0.00 0.67 0.41 0.140448031076 The Andersons, Inc. (0448031076) P001 Shot Blast Baghouse Stack 277764.15 4605250.22 19.49 389.71 No 0.00 0.02 0.00 0.000448031076 The Andersons, Inc. (0448031076) K001 Curing Booth Fugitive Release 277764.15 4605250.22 19.49 389.71 No 0.00 0.67 0.41 0.140448031076 The Andersons, Inc. (0448031076) F001 Fugitive emissions from railcar degassing and c;lea 277764.15 4605250.22 19.49 389.71 No 0.00 0.71 0.00 0.000448031076 Total 19.49 389.71 100.00 100.00 100.00 100.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0387040001 Bulk Molding Compounds, Inc. (0387040001) P011 DFBS 279353.55 4603134.11 19.57 391.44 Yes 0.88 6.57 0.00 0.000387040001 Bulk Molding Compounds, Inc. (0387040001) P013 DFBS 279353.55 4603134.11 19.57 391.44 Yes 5.26 5.26 0.00 0.000387040001 Bulk Molding Compounds, Inc. (0387040001) P023 DFBS 279353.55 4603134.11 19.57 391.44 Yes 17.96 17.96 0.00 0.000387040001 Bulk Molding Compounds, Inc. (0387040001) P025 DFBS 279353.55 4603134.11 19.57 391.44 Yes 0.66 0.66 0.00 0.000387040001 Bulk Molding Compounds, Inc. (0387040001) P011 BuildingAir 279353.55 4603134.11 19.57 391.44 Yes 6.57 6.57 0.00 0.000387040001 Bulk Molding Compounds, Inc. (0387040001) P013 BuildingAir 279353.55 4603134.11 19.57 391.44 Yes 5.26 5.26 0.00 0.000387040001 Total 19.57 391.44 36.57 42.27 0.00 0.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0362000079 Graymont Dolime (OH), Inc. (0362000079) P010 Kiln Stack 303860.85 4597980.26 21.01 420.25 Yes 145.99 145.99 150.13 225.630362000079 Graymont Dolime (OH), Inc. (0362000079) P014 Kiln Stack 303860.85 4597980.26 21.01 420.25 Yes 145.99 145.99 148.91 223.780362000079 Graymont Dolime (OH), Inc. (0362000079) P015 Kiln Stack 303860.85 4597980.26 21.01 420.25 Yes 145.99 145.99 154.67 232.440362000079 Graymont Dolime (OH), Inc. (0362000079) P005 P005DC1 303860.85 4597980.26 21.01 420.25 Yes 14.42 14.42 0.00 0.000362000079 Graymont Dolime (OH), Inc. (0362000079) P005 P005DC2 303860.85 4597980.26 21.01 420.25 Yes 14.42 14.42 0.00 0.000362000079 Graymont Dolime (OH), Inc. (0362000079) P005 P005DC3 303860.85 4597980.26 21.01 420.25 Yes 14.42 14.42 0.00 0.000362000079 Graymont Dolime (OH), Inc. (0362000079) P006 Shaffer ATM Hydrator Scrubber Stack - integral pa 303860.85 4597980.26 21.01 420.25 Yes 44.59 44.59 0.00 0.000362000079 Graymont Dolime (OH), Inc. (0362000079) P006 P006DC 303860.85 4597980.26 21.01 420.25 Yes 1.50 1.82 0.00 0.000362000079 Graymont Dolime (OH), Inc. (0362000079) P016 #1, #2, #3 Autoclave Pressure Hydrator Scrubber S 303860.85 4597980.26 21.01 420.25 Yes 1.41 1.76 0.00 0.000362000079 Graymont Dolime (OH), Inc. (0362000079) P020 #1, #2, #3 Autoclave Pressure Hydrator Scrubber S 303860.85 4597980.26 21.01 420.25 Yes 1.34 1.68 0.00 0.000362000079 Graymont Dolime (OH), Inc. (0362000079) P021 P021DC 303860.85 4597980.26 21.01 420.25 Yes 32.81 32.81 0.00 0.000362000079 Graymont Dolime (OH), Inc. (0362000079) P901 P901DC 303860.85 4597980.26 21.01 420.25 Yes 0.94 1.16 0.00 0.000362000079 Graymont Dolime (OH), Inc. (0362000079) F004 F004FUG 303860.85 4597980.26 21.01 420.25 Yes 0.40 2.66 0.00 0.000362000079 Graymont Dolime (OH), Inc. (0362000079) F007 F007FUG 303860.85 4597980.26 21.01 420.25 Yes 0.61 5.84 0.00 0.000362000079 Graymont Dolime (OH), Inc. (0362000079) F008 F008FUG 303860.85 4597980.26 21.01 420.25 Yes 0.24 1.30 0.00 0.000362000079 Graymont Dolime (OH), Inc. (0362000079) F009 F009FUG 303860.85 4597980.26 21.01 420.25 Yes 0.47 1.41 0.00 0.000362000079 Graymont Dolime (OH), Inc. (0362000079) P901 P901FUG 303860.85 4597980.26 21.01 420.25 Yes 0.18 0.22 0.00 0.000362000079 Total 21.01 420.25 565.70 576.48 453.70 681.85 N N N N NA NA NA NA Model Model Model Model Yes Yes Yes Yes0387000377 Troy Energy, LLC (0387000377) P001 P001 294515.42 4594616.84 21.79 435.89 Yes 68.77 68.77 254.43 123.780387000377 Troy Energy, LLC (0387000377) P002 P002 294515.42 4594616.84 21.79 435.89 Yes 68.77 68.77 254.43 123.780387000377 Troy Energy, LLC (0387000377) P003 P003 294515.42 4594616.84 21.79 435.89 Yes 68.77 68.77 254.43 123.780387000377 Troy Energy, LLC (0387000377) P004 P004 294515.42 4594616.84 21.79 435.89 Yes 68.77 68.77 254.43 123.780387000377 Troy Energy, LLC (0387000377) P005 P005 294515.42 4594616.84 21.79 435.89 Yes 2.90 2.90 19.41 101.400387000377 Troy Energy, LLC (0387000377) P006 P006 294515.42 4594616.84 21.79 435.89 Yes 2.90 2.90 19.41 101.400387000377 Total 21.79 435.89 280.86 280.86 1056.56 697.91 N N N N NA NA NA NA Screen Screen Model Model No No Yes Yes0372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P010 P010,13,14 302362.9 4593267.7 24.68 493.66 Yes 35.83 38.13 275.35 133.240372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P013 P010,13,14 302362.9 4593267.7 24.68 493.66 Yes 32.75 34.85 251.62 121.750372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P014 P010,13,14 302362.9 4593267.7 24.68 493.66 Yes 37.96 40.39 291.65 141.120372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P015 P015 #1ESP 302362.9 4593267.7 24.68 493.66 Yes 72.14 86.86 582.13 54.410372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P019 P019 Baghouse Stack 302362.9 4593267.7 24.68 493.66 Yes 18.29 20.63 626.09 66.750372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P030 P030 (0844) 302362.9 4593267.7 24.68 493.66 Yes 35.65 35.65 3.45 2.900372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P902 P902 302362.9 4593267.7 24.68 493.66 Yes 37.80 37.80 673.43 328.500372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) F003 F003 (1103) 302362.9 4593267.7 24.68 493.66 Yes 0.04 0.12 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) F004 F004 (1044) 302362.9 4593267.7 24.68 493.66 Yes 0.26 0.61 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) F004 F004 (1045) 302362.9 4593267.7 24.68 493.66 Yes 0.26 0.61 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) F007 F007/P004 (0733) 302362.9 4593267.7 24.68 493.66 Yes 1.70 4.21 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P004 F007/P004 (0733) 302362.9 4593267.7 24.68 493.66 Yes 6.57 6.57 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P004 P004 (0700) 302362.9 4593267.7 24.68 493.66 Yes 6.57 6.57 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P004 P004 (0731) 302362.9 4593267.7 24.68 493.66 Yes 6.57 6.57 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P004 P004 (0732) 302362.9 4593267.7 24.68 493.66 Yes 6.57 6.57 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P004 P004 (0734) 302362.9 4593267.7 24.68 493.66 Yes 6.57 6.57 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P004 P004 (1144) 302362.9 4593267.7 24.68 493.66 Yes 6.57 6.57 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P004 P004 (1145) 302362.9 4593267.7 24.68 493.66 Yes 6.57 6.57 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P008 P008 (0715) 302362.9 4593267.7 24.68 493.66 Yes 0.56 1.17 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P027 P027 (1088) 302362.9 4593267.7 24.68 493.66 Yes 26.98 26.98 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P027 P027 (1104) 302362.9 4593267.7 24.68 493.66 Yes 26.98 26.98 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P029 P029 (1140) 302362.9 4593267.7 24.68 493.66 Yes 0.74 1.15 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P902 Kiln 7 Discharge End - Cooler Feeder Dust Collecto 302362.9 4593267.7 24.68 493.66 Yes 22.71 26.44 379.76 26.340372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P903 P903 (1156) 302362.9 4593267.7 24.68 493.66 Yes 0.32 1.12 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) F001 F001-Roadwy 302362.90 4593267.70 24.68 493.66 Yes 1.21 8.86 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) F002 F002-Piles 302362.90 4593267.70 24.68 493.66 Yes 2.84 18.77 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) F003 South Lime Storage and Loadout - Lime Handling F 302362.90 4593267.70 24.68 493.66 Yes 0.82 2.37 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) F003 South Lime Storage and Loadout - Lime Loading Fu 302362.90 4593267.70 24.68 493.66 Yes 0.61 1.77 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) F004 South Plant Dust Load-out - Truck Loading Fugitive 302362.90 4593267.70 24.68 493.66 Yes 0.52 1.23 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) F005 F005 Fugitive Egress Point 302362.90 4593267.70 24.68 493.66 Yes 9.79 9.79 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) F007 North Plant Lime Loadout - Handling Fugitives 302362.90 4593267.70 24.68 493.66 Yes 2.08 5.15 0.00 0.00

Page 311: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx CO0372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) F007 North Plant Lime Loadout - Screening Fugitives 302362.90 4593267.70 24.68 493.66 Yes 3.78 9.36 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) F007 North Plant Lime Loadout - Loading Fugitives 302362.90 4593267.70 24.68 493.66 Yes 3.78 9.36 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) F008 F008-Min.Ex 302362.90 4593267.70 24.68 493.66 Yes 4.09 17.80 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) F008 F008 Drill 302362.90 4593267.70 24.68 493.66 Yes 4.09 17.80 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P004 North Plant Lime Screening & Briquetting - Handli 302362.90 4593267.70 24.68 493.66 Yes 6.57 6.57 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P008 North Plant Coal Crushing and Screening - Handlin 302362.90 4593267.70 24.68 493.66 Yes 0.55 1.16 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P008 North Plant Coal Crushing and Screening - Unload 302362.90 4593267.70 24.68 493.66 Yes 0.56 1.17 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P010 #5 Kiln - Handling Fugitives 302362.90 4593267.70 24.68 493.66 Yes 35.83 38.13 275.35 133.240372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P013 #4 Kiln - Handling Fugitives 302362.90 4593267.70 24.68 493.66 Yes 32.75 34.85 251.62 121.750372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P014 #6 Kiln - Handling Fugitives 302362.90 4593267.70 24.68 493.66 Yes 37.96 40.39 291.65 141.120372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P015 #1 Kiln - Screening Fugitives 302362.90 4593267.70 24.68 493.66 Yes 72.14 86.86 582.13 54.410372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P015 #1 Kiln - Handling Fugitives 302362.90 4593267.70 24.68 493.66 Yes 72.14 86.86 582.13 54.410372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P018 P018 Fugitive Egress Point 302362.90 4593267.70 24.68 493.66 Yes 2.50 5.24 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P019 #2 Kiln - Screening Fugitives 302362.90 4593267.70 24.68 493.66 Yes 18.29 20.63 626.09 66.750372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P019 #2 Kiln - Handling Fugitives 302362.90 4593267.70 24.68 493.66 Yes 18.29 20.63 626.09 66.750372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P029 MgO Plant Dryer - Handling Fugitives 302362.90 4593267.70 24.68 493.66 Yes 0.74 1.15 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P902 #7 Kiln - Stone Handling Fugitives 302362.90 4593267.70 24.68 493.66 Yes 22.71 26.44 379.76 26.340372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P903 302362.90 4593267.70 24.68 493.66 Yes 0.21 0.37 0.00 0.000372000127 MARTIN MARIETTA MAGNESIA SPECIALTIES INC. (0372000127) P904 302362.90 4593267.70 24.68 493.66 Yes 0.98 1.81 0.00 0.000372000127 Total 24.68 493.66 752.70 904.16 6698.28 1539.74 N N N N NA NA NA NA Model Model Model Model Yes Yes Yes YesN3849 STONECO, INC Non-Metallic Mineral Crusher 298000.00 4640600.00 24.57 491.47 30.00 30.00 0.00 0.00N3849 STONECO INC DENNISTON QUARRY 298000.00 4640600.00 24.57 491.47 No 78.77 78.77 0.00 0.00N3849 STONECO, INC Non-Metallic Mineral Crusher 298000.00 4640600.00 24.57 491.47 30.00 30.00 0.00 0.00N3849 Total 24.57 491.47 138.77 138.77 0.00 0.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoN5778 GERKEN MATERIALS INC PLANT #15 BAGHOUSE STACK 298000.00 4640600.00 24.57 491.47 1.92 1.92 5.52 25.04N5778 Total 24.57 491.47 1.92 1.92 5.52 25.04 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P001 322 273939.15 4601325.94 24.89 497.78 Yes 73.39 73.39 69.20 8.230448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P013 322 273939.15 4601325.94 24.89 497.78 Yes 76.71 76.71 72.64 8.690448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P013 316 273939.15 4601325.94 24.89 497.78 Yes 8.07 8.07 22.85 0.720448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P013 317 273939.15 4601325.94 24.89 497.78 Yes 8.07 8.07 22.85 0.720448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P013 318 273939.15 4601325.94 24.89 497.78 Yes 8.07 8.07 22.85 0.720448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P013 345 273939.15 4601325.94 24.89 497.78 Yes 8.07 8.07 22.85 0.720448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P013 346 273939.15 4601325.94 24.89 497.78 Yes 8.07 8.07 22.85 0.720448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P015 P015,DCSCR 273939.15 4601325.94 24.89 497.78 Yes 1.91 3.85 11.81 1.110448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P015 P015,TO 273939.15 4601325.94 24.89 497.78 Yes 1.69 1.69 11.81 0.990448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P045 A3 273939.15 4601325.94 24.89 497.78 Yes 3.60 3.60 0.11 0.080448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P046 273939.15 4601325.94 24.89 497.78 Yes 0.92 0.92 0.00 0.000448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P047 273939.15 4601325.94 24.89 497.78 Yes 0.92 0.92 0.00 0.000448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P048 273939.15 4601325.94 24.89 497.78 Yes 0.92 0.92 0.00 0.000448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P049 273939.15 4601325.94 24.89 497.78 Yes 0.92 0.92 0.00 0.000448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P050 273939.15 4601325.94 24.89 497.78 Yes 0.92 0.92 0.00 0.000448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P051 273939.15 4601325.94 24.89 497.78 Yes 0.92 0.92 0.00 0.000448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P052 273939.15 4601325.94 24.89 497.78 Yes 0.92 0.92 0.00 0.000448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P017 273939.15 4601325.94 24.89 497.78 Yes 4.86 4.86 1.18 1.010448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P026 273939.15 4601325.94 24.89 497.78 Yes 0.19 0.19 0.65 0.540448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P033 273939.15 4601325.94 24.89 497.78 Yes 4.56 4.56 0.00 0.000448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P058 P058 273939.15 4601325.94 24.89 497.78 Yes 13.68 13.68 0.29 0.240448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P061 347 273939.15 4601325.94 24.89 497.78 Yes 4.44 4.44 0.55 0.460448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P062 348 273939.15 4601325.94 24.89 497.78 Yes 5.04 5.04 0.55 0.460448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P063 349 273939.15 4601325.94 24.89 497.78 Yes 3.84 3.84 0.55 0.460448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P064 304 273939.15 4601325.94 24.89 497.78 Yes 5.04 5.04 0.55 0.460448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P069 P054/P056 273939.15 4601325.94 24.89 497.78 Yes 13.68 13.68 0.38 0.320448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P070 P055/P057 273939.15 4601325.94 24.89 497.78 Yes 13.68 13.68 0.34 0.290448000012 Johns Manville / Plant #01 - wtv1 (0448000012) F004 F004/5, 333 273939.15 4601325.94 24.89 497.78 Yes 2.53 2.53 0.00 0.000448000012 Johns Manville / Plant #01 - wtv1 (0448000012) F004 F004/5, 334 273939.15 4601325.94 24.89 497.78 Yes 2.53 2.53 0.00 0.000448000012 Johns Manville / Plant #01 - wtv1 (0448000012) F004 F004/5, 335 273939.15 4601325.94 24.89 497.78 Yes 2.53 2.53 0.00 0.000448000012 Johns Manville / Plant #01 - wtv1 (0448000012) F004 F004/5, 336 273939.15 4601325.94 24.89 497.78 Yes 2.53 2.53 0.00 0.000448000012 Johns Manville / Plant #01 - wtv1 (0448000012) F004 F004/5, 337 273939.15 4601325.94 24.89 497.78 Yes 2.53 2.53 0.00 0.000448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P001 002 273939.15 4601325.94 24.89 497.78 Yes 73.39 73.39 69.20 8.230448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P001 003 273939.15 4601325.94 24.89 497.78 Yes 73.39 73.39 69.20 8.230448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P001 004 273939.15 4601325.94 24.89 497.78 Yes 8.64 8.64 5.34 0.330448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P001 005 273939.15 4601325.94 24.89 497.78 Yes 8.64 8.64 5.34 0.330448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P001 006 273939.15 4601325.94 24.89 497.78 Yes 8.64 8.64 5.34 0.330448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P001 A6 273939.15 4601325.94 24.89 497.78 Yes 43.22 43.22 26.71 1.650448000012 Johns Manville / Plant #01 - wtv1 (0448000012) P013 A14 273939.15 4601325.94 24.89 497.78 Yes 76.71 76.71 72.64 8.690448000012 Johns Manville / Plant #01 - wtv1 (0448000012) F004 Silo to Scale Transfer 273939.15 4601325.94 24.89 497.78 Yes 1.40 1.40 0.00 0.000448000012 Total 24.89 497.78 579.76 581.71 538.60 54.76 N N N N NA NA NA NA Model Model Model Screen Yes Yes Yes NoB2063 Faurecia Interior Systems Saline, LLC 271557.00 4627931.00 25.01 500.14 6.68 6.68 140.60 30.92B2063 Faurecia Interior Systems Saline, LLC EUAutoPlasCoatLn (Spray Booth) 271557.00 4627931.00 25.01 500.14 0.00 0.02 12.98 4.74B2063 Faurecia Interior Systems Saline, LLC EUAutoPlasCoatLn-02 (Cure Oven) 271557.00 4627931.00 25.01 500.14 0.00 0.02 12.98 4.74B2063 AUTOMOTIVE COMPONENTS HOLDINGS, LLC 3 PLASTIC AUTO PARTS COATING LIN 271557.00 4627931.00 25.01 500.14 8.76 8.76 12.98 4.74B2063 Faurecia Interior Systems Saline, LLC 271557.00 4627931.00 25.01 500.14 6.68 6.68 140.60 30.92B2063 AUTOMOTIVE COMPONENTS HOLDINGS, LLC 3 PLASTIC AUTO PARTS COATING LIN 271557.00 4627931.00 25.01 500.14 8.76 8.76 12.98 4.74B2063 Total 25.01 500.14 30.88 30.92 333.14 80.80 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoB4311 COUNTRYMARK COOPERATIVE, INC GRAIN DRYER 270766.00 4627257.00 25.42 508.33 0.00 0.00 0.00 0.00B4311 ADM GRAIN CO 270766.00 4627257.00 25.42 508.33 No 80.64 80.64 31.09 31.09B4311 COUNTRYMARK COOPERATIVE, INC GRAIN DRYER 270766.00 4627257.00 25.42 508.33 0.00 0.00 0.00 0.00

Page 312: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx COB4311 Total 25.42 508.33 80.64 80.64 31.09 31.09 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0448000013 Johns Manville - Waterville 07 (0448000013) P014 P13 Whitewater Vacuum Stack 272988.87 4600614.48 26.08 521.52 Yes 5.26 5.26 3.20 7.880448000013 Johns Manville - Waterville 07 (0448000013) P014 Basement Stack 5 272988.87 4600614.48 26.08 521.52 Yes 0.19 0.19 0.49 0.430448000013 Johns Manville - Waterville 07 (0448000013) P014 Hydroformer Stack 10 272988.87 4600614.48 26.08 521.52 Yes 0.19 0.19 0.49 0.430448000013 Johns Manville - Waterville 07 (0448000013) P014 Applicator Stack 11 272988.87 4600614.48 26.08 521.52 Yes 0.19 0.19 0.49 0.430448000013 Johns Manville - Waterville 07 (0448000013) P014 Applicator Stack 12 272988.87 4600614.48 26.08 521.52 Yes 0.19 0.19 0.49 0.430448000013 Johns Manville - Waterville 07 (0448000013) P018 (40A)ClnGas 272988.87 4600614.48 26.08 521.52 Yes 8.41 8.41 0.08 9.320448000013 Johns Manville - Waterville 07 (0448000013) P018 (41)Ducon 5 272988.87 4600614.48 26.08 521.52 Yes 4.51 4.57 0.08 9.600448000013 Johns Manville - Waterville 07 (0448000013) P018 Ducon 4 272988.87 4600614.48 26.08 521.52 Yes 4.38 4.43 0.08 9.320448000013 Johns Manville - Waterville 07 (0448000013) P019 (40A)ClnGas 272988.87 4600614.48 26.08 521.52 Yes 9.72 9.72 0.06 6.940448000013 Johns Manville - Waterville 07 (0448000013) P019 (41)Ducon 5 272988.87 4600614.48 26.08 521.52 Yes 2.68 2.82 0.06 7.150448000013 Johns Manville - Waterville 07 (0448000013) P019 Ducon 4 272988.87 4600614.48 26.08 521.52 Yes 2.60 2.74 0.06 6.940448000013 Johns Manville - Waterville 07 (0448000013) P036 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P036 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P036 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P036 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P036 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P037 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P037 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P037 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P037 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P037 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P038 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P038 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P038 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P038 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P038 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P039 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P039 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P039 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P039 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P039 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P042 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P042 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P042 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P042 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P042 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P043 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P043 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P043 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P043 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P043 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P045 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P045 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P045 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P045 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P045 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P047 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P047 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P047 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P047 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P047 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P048 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P048 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P048 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P048 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P048 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P049 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P049 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P049 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P049 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P049 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P050 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P050 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P050 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P050 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P050 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P051 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P051 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P051 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P051 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P051 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.590448000013 Johns Manville - Waterville 07 (0448000013) P053 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P053 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P053 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P053 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P053 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.07

Page 313: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx CO0448000013 Johns Manville - Waterville 07 (0448000013) P054 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P054 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P054 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P054 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P054 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P055 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P055 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P055 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P055 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P055 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P056 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.190448000013 Johns Manville - Waterville 07 (0448000013) P056 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.190448000013 Johns Manville - Waterville 07 (0448000013) P056 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.190448000013 Johns Manville - Waterville 07 (0448000013) P056 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.190448000013 Johns Manville - Waterville 07 (0448000013) P056 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.190448000013 Johns Manville - Waterville 07 (0448000013) P058 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.190448000013 Johns Manville - Waterville 07 (0448000013) P058 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.190448000013 Johns Manville - Waterville 07 (0448000013) P058 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.190448000013 Johns Manville - Waterville 07 (0448000013) P058 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.190448000013 Johns Manville - Waterville 07 (0448000013) P058 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.190448000013 Johns Manville - Waterville 07 (0448000013) P059 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P059 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P059 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P059 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P059 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P061 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P061 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P061 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P061 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P061 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P062 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P062 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P062 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P062 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P062 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P064 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P064 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P064 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P064 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P064 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.08 0.08 0.07 2.070448000013 Johns Manville - Waterville 07 (0448000013) P086 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.11 3.100448000013 Johns Manville - Waterville 07 (0448000013) P086 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.11 3.100448000013 Johns Manville - Waterville 07 (0448000013) P086 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.11 3.100448000013 Johns Manville - Waterville 07 (0448000013) P086 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.11 3.100448000013 Johns Manville - Waterville 07 (0448000013) P086 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.11 3.100448000013 Johns Manville - Waterville 07 (0448000013) P088 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.11 3.100448000013 Johns Manville - Waterville 07 (0448000013) P088 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.11 3.100448000013 Johns Manville - Waterville 07 (0448000013) P088 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.11 3.100448000013 Johns Manville - Waterville 07 (0448000013) P088 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.11 3.100448000013 Johns Manville - Waterville 07 (0448000013) P088 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.11 3.100448000013 Johns Manville - Waterville 07 (0448000013) P089 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.10 3.360448000013 Johns Manville - Waterville 07 (0448000013) P089 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.10 3.360448000013 Johns Manville - Waterville 07 (0448000013) P089 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.10 3.360448000013 Johns Manville - Waterville 07 (0448000013) P089 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.10 3.360448000013 Johns Manville - Waterville 07 (0448000013) P089 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.10 3.360448000013 Johns Manville - Waterville 07 (0448000013) P091 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.10 3.360448000013 Johns Manville - Waterville 07 (0448000013) P091 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.10 3.360448000013 Johns Manville - Waterville 07 (0448000013) P091 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.10 3.360448000013 Johns Manville - Waterville 07 (0448000013) P091 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.10 3.360448000013 Johns Manville - Waterville 07 (0448000013) P091 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.10 3.360448000013 Johns Manville - Waterville 07 (0448000013) P092 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.09 3.560448000013 Johns Manville - Waterville 07 (0448000013) P092 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.10 0.10 0.09 3.560448000013 Johns Manville - Waterville 07 (0448000013) P092 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.10 0.10 0.09 3.560448000013 Johns Manville - Waterville 07 (0448000013) P092 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.10 0.10 0.09 3.560448000013 Johns Manville - Waterville 07 (0448000013) P092 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.10 0.10 0.09 3.560448000013 Johns Manville - Waterville 07 (0448000013) P094 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.09 3.560448000013 Johns Manville - Waterville 07 (0448000013) P094 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.10 0.10 0.09 3.560448000013 Johns Manville - Waterville 07 (0448000013) P094 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.10 0.10 0.09 3.560448000013 Johns Manville - Waterville 07 (0448000013) P094 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.10 0.10 0.09 3.560448000013 Johns Manville - Waterville 07 (0448000013) P094 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.10 0.10 0.09 3.560448000013 Johns Manville - Waterville 07 (0448000013) P095 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.08 3.640448000013 Johns Manville - Waterville 07 (0448000013) P095 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.09 0.09 0.08 3.640448000013 Johns Manville - Waterville 07 (0448000013) P095 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.09 0.09 0.08 3.640448000013 Johns Manville - Waterville 07 (0448000013) P095 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.09 0.09 0.08 3.640448000013 Johns Manville - Waterville 07 (0448000013) P095 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.09 0.09 0.08 3.640448000013 Johns Manville - Waterville 07 (0448000013) P097 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.08 3.640448000013 Johns Manville - Waterville 07 (0448000013) P097 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.09 0.09 0.08 3.64

Page 314: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx CO0448000013 Johns Manville - Waterville 07 (0448000013) P097 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.09 0.09 0.08 3.640448000013 Johns Manville - Waterville 07 (0448000013) P097 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.09 0.09 0.08 3.640448000013 Johns Manville - Waterville 07 (0448000013) P097 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.09 0.09 0.08 3.640448000013 Johns Manville - Waterville 07 (0448000013) P098 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P098 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P098 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P098 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P098 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P100 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P100 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P100 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P100 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P100 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P101 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P101 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P101 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P101 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P101 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P103 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P103 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P103 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P103 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P103 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 3.750448000013 Johns Manville - Waterville 07 (0448000013) P104 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.02 1.050448000013 Johns Manville - Waterville 07 (0448000013) P104 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.02 0.02 0.02 1.050448000013 Johns Manville - Waterville 07 (0448000013) P104 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.02 0.02 0.02 1.050448000013 Johns Manville - Waterville 07 (0448000013) P104 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.02 0.02 0.02 1.050448000013 Johns Manville - Waterville 07 (0448000013) P104 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.02 0.02 0.02 1.050448000013 Johns Manville - Waterville 07 (0448000013) P105 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.02 1.050448000013 Johns Manville - Waterville 07 (0448000013) P105 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.02 0.02 0.02 1.050448000013 Johns Manville - Waterville 07 (0448000013) P105 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.02 0.02 0.02 1.050448000013 Johns Manville - Waterville 07 (0448000013) P105 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.02 0.02 0.02 1.050448000013 Johns Manville - Waterville 07 (0448000013) P105 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.02 0.02 0.02 1.050448000013 Johns Manville - Waterville 07 (0448000013) P106 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.02 1.050448000013 Johns Manville - Waterville 07 (0448000013) P106 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.02 0.02 0.02 1.050448000013 Johns Manville - Waterville 07 (0448000013) P106 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.02 0.02 0.02 1.050448000013 Johns Manville - Waterville 07 (0448000013) P106 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.02 0.02 0.02 1.050448000013 Johns Manville - Waterville 07 (0448000013) P106 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.02 0.02 0.02 1.050448000013 Johns Manville - Waterville 07 (0448000013) P107 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.01 1.660448000013 Johns Manville - Waterville 07 (0448000013) P107 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.01 0.01 0.01 1.660448000013 Johns Manville - Waterville 07 (0448000013) P107 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.01 0.01 0.01 1.660448000013 Johns Manville - Waterville 07 (0448000013) P107 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.01 0.01 0.01 1.660448000013 Johns Manville - Waterville 07 (0448000013) P107 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.01 0.01 0.01 1.660448000013 Johns Manville - Waterville 07 (0448000013) P108 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.01 1.660448000013 Johns Manville - Waterville 07 (0448000013) P108 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.01 0.01 0.01 1.660448000013 Johns Manville - Waterville 07 (0448000013) P108 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.01 0.01 0.01 1.660448000013 Johns Manville - Waterville 07 (0448000013) P108 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.01 0.01 0.01 1.660448000013 Johns Manville - Waterville 07 (0448000013) P108 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.01 0.01 0.01 1.660448000013 Johns Manville - Waterville 07 (0448000013) P109 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.01 1.660448000013 Johns Manville - Waterville 07 (0448000013) P109 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.01 0.01 0.01 1.660448000013 Johns Manville - Waterville 07 (0448000013) P109 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.01 0.01 0.01 1.660448000013 Johns Manville - Waterville 07 (0448000013) P109 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.01 0.01 0.01 1.660448000013 Johns Manville - Waterville 07 (0448000013) P109 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.01 0.01 0.01 1.660448000013 Johns Manville - Waterville 07 (0448000013) P110 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P110 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P110 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P110 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P110 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P111 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P111 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P111 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P111 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P111 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P112 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P112 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P112 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P112 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P112 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P113 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P113 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P113 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P113 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P113 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.11 0.11 0.09 2.940448000013 Johns Manville - Waterville 07 (0448000013) P124 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.03 0.830448000013 Johns Manville - Waterville 07 (0448000013) P124 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.04 0.04 0.03 0.830448000013 Johns Manville - Waterville 07 (0448000013) P124 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.04 0.04 0.03 0.830448000013 Johns Manville - Waterville 07 (0448000013) P124 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.04 0.04 0.03 0.83

Page 315: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx CO0448000013 Johns Manville - Waterville 07 (0448000013) P124 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.04 0.04 0.03 0.830448000013 Johns Manville - Waterville 07 (0448000013) P126 (31)EMC 5 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.03 0.670448000013 Johns Manville - Waterville 07 (0448000013) P126 (32)EMC 3 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 0.670448000013 Johns Manville - Waterville 07 (0448000013) P126 (33)EMC 6 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 0.670448000013 Johns Manville - Waterville 07 (0448000013) P126 (34)EMC 1 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 0.670448000013 Johns Manville - Waterville 07 (0448000013) P126 (34A)EMC 7 272988.87 4600614.48 26.08 521.52 Yes 0.03 0.03 0.03 0.670448000013 Johns Manville - Waterville 07 (0448000013) P127 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P127 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.17 3.050448000013 Johns Manville - Waterville 07 (0448000013) P127 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.17 3.050448000013 Johns Manville - Waterville 07 (0448000013) P127 (61) 29&30 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.17 3.050448000013 Johns Manville - Waterville 07 (0448000013) P128 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P128 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.16 3.050448000013 Johns Manville - Waterville 07 (0448000013) P128 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.16 3.050448000013 Johns Manville - Waterville 07 (0448000013) P128 (61) 29&30 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.16 3.050448000013 Johns Manville - Waterville 07 (0448000013) P129 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P129 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.16 3.050448000013 Johns Manville - Waterville 07 (0448000013) P129 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.16 3.050448000013 Johns Manville - Waterville 07 (0448000013) P129 (61) 29&30 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.16 3.050448000013 Johns Manville - Waterville 07 (0448000013) P130 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P130 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.16 3.050448000013 Johns Manville - Waterville 07 (0448000013) P130 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.16 3.050448000013 Johns Manville - Waterville 07 (0448000013) P130 (61) 29&30 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.16 3.050448000013 Johns Manville - Waterville 07 (0448000013) P131 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P131 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.16 3.050448000013 Johns Manville - Waterville 07 (0448000013) P131 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.16 3.050448000013 Johns Manville - Waterville 07 (0448000013) P131 (61) 29&30 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.16 3.050448000013 Johns Manville - Waterville 07 (0448000013) P134 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P134 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.15 0.15 0.18 2.650448000013 Johns Manville - Waterville 07 (0448000013) P134 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.15 0.15 0.18 2.650448000013 Johns Manville - Waterville 07 (0448000013) P134 (61) 29&30 272988.87 4600614.48 26.08 521.52 Yes 0.15 0.15 0.18 2.650448000013 Johns Manville - Waterville 07 (0448000013) P135 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P135 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.15 0.15 0.18 2.650448000013 Johns Manville - Waterville 07 (0448000013) P135 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.15 0.15 0.18 2.650448000013 Johns Manville - Waterville 07 (0448000013) P135 (61) 29&30 272988.87 4600614.48 26.08 521.52 Yes 0.15 0.15 0.18 2.650448000013 Johns Manville - Waterville 07 (0448000013) P136 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P136 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.15 0.15 0.18 2.650448000013 Johns Manville - Waterville 07 (0448000013) P136 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.15 0.15 0.18 2.650448000013 Johns Manville - Waterville 07 (0448000013) P136 (61) 29&30 272988.87 4600614.48 26.08 521.52 Yes 0.15 0.15 0.18 2.650448000013 Johns Manville - Waterville 07 (0448000013) P137 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P137 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.15 0.15 0.18 2.650448000013 Johns Manville - Waterville 07 (0448000013) P137 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.15 0.15 0.18 2.650448000013 Johns Manville - Waterville 07 (0448000013) P137 (61) 29&30 272988.87 4600614.48 26.08 521.52 Yes 0.15 0.15 0.18 2.650448000013 Johns Manville - Waterville 07 (0448000013) P138 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P138 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.15 0.15 0.18 2.650448000013 Johns Manville - Waterville 07 (0448000013) P138 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.15 0.15 0.18 2.650448000013 Johns Manville - Waterville 07 (0448000013) P138 (61) 29&30 272988.87 4600614.48 26.08 521.52 Yes 0.15 0.15 0.18 2.650448000013 Johns Manville - Waterville 07 (0448000013) P140 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P140 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.19 2.520448000013 Johns Manville - Waterville 07 (0448000013) P140 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.19 2.520448000013 Johns Manville - Waterville 07 (0448000013) P140 (62) 31&32 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.19 2.520448000013 Johns Manville - Waterville 07 (0448000013) P141 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P141 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.19 2.520448000013 Johns Manville - Waterville 07 (0448000013) P141 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.19 2.520448000013 Johns Manville - Waterville 07 (0448000013) P141 (62) 31&32 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.19 2.520448000013 Johns Manville - Waterville 07 (0448000013) P142 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P142 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.19 2.520448000013 Johns Manville - Waterville 07 (0448000013) P142 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.19 2.520448000013 Johns Manville - Waterville 07 (0448000013) P142 (62) 31&32 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.19 2.520448000013 Johns Manville - Waterville 07 (0448000013) P143 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P143 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.19 2.520448000013 Johns Manville - Waterville 07 (0448000013) P143 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.19 2.520448000013 Johns Manville - Waterville 07 (0448000013) P143 (62) 31&32 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.19 2.520448000013 Johns Manville - Waterville 07 (0448000013) P144 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P144 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.19 2.520448000013 Johns Manville - Waterville 07 (0448000013) P144 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.19 2.520448000013 Johns Manville - Waterville 07 (0448000013) P144 (62) 31&32 272988.87 4600614.48 26.08 521.52 Yes 0.12 0.12 0.19 2.520448000013 Johns Manville - Waterville 07 (0448000013) P146 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P146 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.13 0.13 0.20 2.280448000013 Johns Manville - Waterville 07 (0448000013) P146 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.13 0.13 0.20 2.280448000013 Johns Manville - Waterville 07 (0448000013) P146 (62) 31&32 272988.87 4600614.48 26.08 521.52 Yes 0.13 0.13 0.20 2.280448000013 Johns Manville - Waterville 07 (0448000013) P147 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P147 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.13 0.13 0.20 2.280448000013 Johns Manville - Waterville 07 (0448000013) P147 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.13 0.13 0.20 2.280448000013 Johns Manville - Waterville 07 (0448000013) P147 (62) 31&32 272988.87 4600614.48 26.08 521.52 Yes 0.13 0.13 0.20 2.280448000013 Johns Manville - Waterville 07 (0448000013) P148 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P148 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.13 0.13 0.20 2.280448000013 Johns Manville - Waterville 07 (0448000013) P148 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.13 0.13 0.20 2.28

Page 316: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx CO0448000013 Johns Manville - Waterville 07 (0448000013) P148 (62) 31&32 272988.87 4600614.48 26.08 521.52 Yes 0.13 0.13 0.20 2.280448000013 Johns Manville - Waterville 07 (0448000013) P149 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P149 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.13 0.13 0.20 2.280448000013 Johns Manville - Waterville 07 (0448000013) P149 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.13 0.13 0.20 2.280448000013 Johns Manville - Waterville 07 (0448000013) P149 (62) 31&32 272988.87 4600614.48 26.08 521.52 Yes 0.13 0.13 0.20 2.280448000013 Johns Manville - Waterville 07 (0448000013) P150 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P150 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.13 0.13 0.20 2.280448000013 Johns Manville - Waterville 07 (0448000013) P150 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.13 0.13 0.20 2.280448000013 Johns Manville - Waterville 07 (0448000013) P150 (62) 31&32 272988.87 4600614.48 26.08 521.52 Yes 0.13 0.13 0.20 2.280448000013 Johns Manville - Waterville 07 (0448000013) P152 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P152 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.21 2.570448000013 Johns Manville - Waterville 07 (0448000013) P152 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.21 2.570448000013 Johns Manville - Waterville 07 (0448000013) P152 (63) 33&34 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.21 2.570448000013 Johns Manville - Waterville 07 (0448000013) P153 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P153 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.21 2.570448000013 Johns Manville - Waterville 07 (0448000013) P153 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.21 2.570448000013 Johns Manville - Waterville 07 (0448000013) P153 (63) 33&34 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.21 2.570448000013 Johns Manville - Waterville 07 (0448000013) P154 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P154 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.21 2.570448000013 Johns Manville - Waterville 07 (0448000013) P154 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.21 2.570448000013 Johns Manville - Waterville 07 (0448000013) P154 (63) 33&34 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.21 2.570448000013 Johns Manville - Waterville 07 (0448000013) P155 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P155 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.21 2.570448000013 Johns Manville - Waterville 07 (0448000013) P155 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.21 2.570448000013 Johns Manville - Waterville 07 (0448000013) P155 (63) 33&34 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.21 2.570448000013 Johns Manville - Waterville 07 (0448000013) P156 (38)Ducon 1 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P156 (39)Ducon 2 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.21 2.570448000013 Johns Manville - Waterville 07 (0448000013) P156 (40)Ducon 3 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.21 2.570448000013 Johns Manville - Waterville 07 (0448000013) P156 (63) 33&34 272988.87 4600614.48 26.08 521.52 Yes 0.14 0.14 0.21 2.570448000013 Johns Manville - Waterville 07 (0448000013) P158 (63) 33&34 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P159 (63) 33&34 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P160 (63) 33&34 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P161 (63) 33&34 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P162 (63) 33&34 272988.87 4600614.48 26.08 521.52 Yes 2.41 2.41 0.92 27.330448000013 Johns Manville - Waterville 07 (0448000013) P239 (40A)ClnGas 272988.87 4600614.48 26.08 521.52 Yes 9.72 9.72 0.39 79.720448000013 Johns Manville - Waterville 07 (0448000013) P239 (41)Ducon 5 272988.87 4600614.48 26.08 521.52 Yes 0.81 0.84 0.02 1.940448000013 Johns Manville - Waterville 07 (0448000013) P239 Ducon 4 272988.87 4600614.48 26.08 521.52 Yes 0.78 0.81 0.02 1.880448000013 Johns Manville - Waterville 07 (0448000013) P240 (40A)ClnGas 272988.87 4600614.48 26.08 521.52 Yes 9.72 9.72 0.39 79.720448000013 Johns Manville - Waterville 07 (0448000013) P240 (41)Ducon 5 272988.87 4600614.48 26.08 521.52 Yes 1.41 1.49 0.04 3.720448000013 Johns Manville - Waterville 07 (0448000013) P240 Ducon 4 272988.87 4600614.48 26.08 521.52 Yes 1.37 1.44 0.04 3.610448000013 Total 26.08 521.52 265.88 266.49 62.35 1813.78 N N N N NA NA NA NA Screen Screen Screen Model No No No Yes0448002007 REXAM Beverage Can Co (0448002007) B004 EP01-1 270313.17 4604033.74 26.49 529.89 Yes 0.01 0.01 0.20 0.170448002007 REXAM Beverage Can Co (0448002007) B004 EP01-3 270313.17 4604033.74 26.49 529.89 Yes 0.01 0.01 0.20 0.170448002007 REXAM Beverage Can Co (0448002007) B005 EP01-2 270313.17 4604033.74 26.49 529.89 Yes 0.01 0.01 0.09 0.070448002007 REXAM Beverage Can Co (0448002007) B005 EP02-1 270313.17 4604033.74 26.49 529.89 Yes 0.01 0.01 0.09 0.070448002007 REXAM Beverage Can Co (0448002007) B005 EP02-2 270313.17 4604033.74 26.49 529.89 Yes 0.01 0.01 0.09 0.070448002007 REXAM Beverage Can Co (0448002007) B005 EP03-2 270313.17 4604033.74 26.49 529.89 Yes 0.01 0.01 0.09 0.070448002007 REXAM Beverage Can Co (0448002007) K009 EP05-1 270313.17 4604033.74 26.49 529.89 Yes 0.06 0.06 0.26 0.220448002007 REXAM Beverage Can Co (0448002007) K009 EP05-2 270313.17 4604033.74 26.49 529.89 Yes 0.06 0.06 0.26 0.220448002007 REXAM Beverage Can Co (0448002007) K009 EP06-1 270313.17 4604033.74 26.49 529.89 Yes 0.06 0.06 0.26 0.220448002007 REXAM Beverage Can Co (0448002007) K009 EP07-1 270313.17 4604033.74 26.49 529.89 Yes 0.06 0.06 0.26 0.220448002007 REXAM Beverage Can Co (0448002007) K009 EP08-1 270313.17 4604033.74 26.49 529.89 Yes 0.06 0.06 0.26 0.220448002007 REXAM Beverage Can Co (0448002007) K010 EP28 270313.17 4604033.74 26.49 529.89 Yes 1.45 1.45 1.29 1.040448002007 REXAM Beverage Can Co (0448002007) K011 EP04-5 270313.17 4604033.74 26.49 529.89 Yes 1.49 1.49 3.42 2.890448002007 REXAM Beverage Can Co (0448002007) K011 EP05-5 270313.17 4604033.74 26.49 529.89 Yes 1.49 1.49 3.42 2.890448002007 REXAM Beverage Can Co (0448002007) K011 EP28 270313.17 4604033.74 26.49 529.89 Yes 1.49 1.49 3.42 2.890448002007 REXAM Beverage Can Co (0448002007) K012 EP28 270313.17 4604033.74 26.49 529.89 Yes 1.23 1.23 4.91 4.160448002007 REXAM Beverage Can Co (0448002007) K009 EP15 270313.17 4604033.74 26.49 529.89 Yes 0.15 0.15 0.65 0.550448002007 REXAM Beverage Can Co (0448002007) K009 EP18 270313.17 4604033.74 26.49 529.89 Yes 0.15 0.15 0.65 0.550448002007 REXAM Beverage Can Co (0448002007) K010 EP16 270313.17 4604033.74 26.49 529.89 Yes 1.45 1.45 0.70 0.560448002007 REXAM Beverage Can Co (0448002007) K010 EP19 270313.17 4604033.74 26.49 529.89 Yes 1.45 1.45 0.70 0.560448002007 REXAM Beverage Can Co (0448002007) K012 EP16-4 270313.17 4604033.74 26.49 529.89 Yes 1.23 1.23 4.91 4.160448002007 REXAM Beverage Can Co (0448002007) K012 EP19-4 270313.17 4604033.74 26.49 529.89 Yes 1.23 1.23 4.91 4.160448002007 REXAM Beverage Can Co (0448002007) K010 FUGITIVE EMISSIONS CONSIDERING 91.8% CE FOR 270313.17 4604033.74 26.49 529.89 Yes 1.45 1.45 0.11 0.090448002007 REXAM Beverage Can Co (0448002007) K011 FUGITIVE EMISSIONS CONSIDERING 91.8% CE FOR 270313.17 4604033.74 26.49 529.89 Yes 1.49 1.49 3.42 2.890448002007 REXAM Beverage Can Co (0448002007) K012 FUGITIVE EMISSIONS CONSIDERING 91.8% CE FOR 270313.17 4604033.74 26.49 529.89 Yes 1.23 1.23 4.91 4.160448002007 Total 26.49 529.89 17.32 17.32 39.43 33.27 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoB7061 Gerdau MacSteel Monroe 1 VTD Dust Silo Vent 304524.00 4640317.00 26.24 524.71 Yes 0.06 0.06 0.00 0.00B7061 Gerdau MacSteel Monroe 2 BULK LIME UNLOADING CAPTURE SYSTEM VENT. 304524.00 4640317.00 26.24 524.71 Yes 0.48 0.48 0.00 0.00B7061 Gerdau MacSteel Monroe 3 VENT FOR LRS STEAM EJECTOR HOTWELL SYSTEM 304524.00 4640317.00 26.24 524.71 Yes 2.77 2.77 3.96 181.41B7061 Gerdau MacSteel Monroe 4 Electric Arc Furnace Baghouse Stack 304524.00 4640317.00 26.24 524.71 Yes 16.29 16.29 36.28 496.88B7061 Gerdau MacSteel Monroe 5 STACK FOR BILLET REHEAT FURNACE 304524.00 4640317.00 26.24 524.71 Yes 0.00 0.05 123.94 24.79B7061 Gerdau MacSteel Monroe 6 STACK FOR LADLE REFINING STATION PACKAGE B 304524.00 4640317.00 26.24 524.71 Yes 0.00 0.05 19.44 16.33B7061 GERDAU MACSTEEL MONROE 7 Reheat furnace 304524.00 4640317.00 26.24 524.71 Yes 0.00 0.05 0.00 0.00B7061 Gerdau MacSteel Monroe 8 304524.00 4640317.00 26.24 524.71 Yes 12.29 12.29 82.44 3.41B7061 Total 26.24 524.71 31.90 32.05 266.06 722.82 N N N N NA NA NA NA Screen Screen Screen Model No No No YesB2816 DTE Electric Company - Monroe Power Plant 252 hp diesel fuel-fired FGD quench pump servicin 305350.00 4640200.00 26.48 529.61 0.43 0.43 6.11 1.32

Page 317: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx COB2816 DTE Electric Company - Monroe Power Plant 252 hp diesel fuel-fired FGD quench pump servicin 305350.00 4640200.00 26.48 529.61 0.43 0.43 6.11 1.32B2816 DTE Electric Company - Monroe Power Plant 252 hp diesel fuel-fired FGD quench pump servicin 305350.00 4640200.00 26.48 529.61 0.43 0.43 6.11 1.32B2816 DTE Electric Company - Monroe Power Plant 252 hp diesel fuel-fired FGD quench pump servicin 305350.00 4640200.00 26.48 529.61 0.43 0.43 6.11 1.32B2816 DTE Electric Company - Monroe Power Plant Unit No. 1 305350.00 4640200.00 26.48 529.61 0.43 0.43 1302.74 599.32B2816 DTE Electric Company - Monroe Power Plant Stack - Boiler No. 1 & Boiler No. 2 305350.00 4640200.00 26.48 529.61 50.85 50.85 8687.95 1174.56B2816 DTE Electric Company - Monroe Power Plant This emission unit represents Limestone handling 305350.00 4640200.00 26.48 529.61 0.52 0.52 0.03 0.01B2816 DTE Electric Company - Monroe Power Plant Unit No. 3 305350.00 4640200.00 26.48 529.61 27.64 27.64 1548.69 626.44B2816 DTE Electric Company - Monroe Power Plant Unit No. 4 305350.00 4640200.00 26.48 529.61 31.10 31.10 1242.83 585.11B2816 DTE Electric Company - Monroe Power Plant Unit No. 2 305350.00 4640200.00 26.48 529.61 50.42 50.42 7385.20 575.24B2816 DTE Electric Company - Monroe Power Plant Diesel Generator Peaking Units DG 11-4 305350.00 4640200.00 26.48 529.61 0.00 0.00 358.64 94.98B2816 DTE Electric Company - Monroe Power Plant Diesel Generator Peaking Units DG 11-5 305350.00 4640200.00 26.48 529.61 0.00 0.00 360.62 95.51B2816 DTE Electric Company - Monroe Power Plant Diesel Generator Peaking Units DG 11-2 305350.00 4640200.00 26.48 529.61 0.00 0.00 363.42 96.25B2816 DTE Electric Company - Monroe Power Plant Diesel Generator Peaking Units DG 11-3 305350.00 4640200.00 26.48 529.61 0.00 0.00 364.79 96.61B2816 DTE Electric Company - Monroe Power Plant Diesel Generator Peaking Units DG 11-1 305350.00 4640200.00 26.48 529.61 0.00 0.00 374.11 99.08B2816 DTE Electric Company - Monroe Power Plant North/South Auxiliary Boiler 305350.00 4640200.00 26.48 529.61 0.00 0.00 363.50 75.73B2816 DTE ELECTRIC COMPANY This stack height applies until the start up of the w 305350.00 4640200.00 26.48 529.61 0.00 0.00 0.03 0.01B2816 DTE Electric Company - Monroe Power Plant 305350.00 4640200.00 26.48 529.61 2913.59 2913.59 142.47 35.12B2816 DETROIT EDISON COMPANY FLY ASH STORAGE & HANDLING 305350.00 4640200.00 26.48 529.61 13.36 13.36 0.03 0.01B2816 Total 26.48 529.61 3089.63 3089.65 22519.52 4159.23 N N N N NA NA NA NA Model Model Model Model Yes Yes Yes YesN2541 MICHIGAN PAVING & MATERIALS COMPANY WASTE OIL FIRED BOILERS 304500.00 4640700.00 26.58 531.51 No 72.71 72.80 0.00 16.21N2541 MICHIGAN PAVING & MATERIALS 304500.00 4640700.00 26.58 531.51 No 0.00 72.80 8.58 16.20N2541 Total 26.58 531.51 72.71 145.60 8.58 32.41 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoN5990 J A JONES ENVIRONMENTAL SERVICES 304600.00 4641500.00 27.35 546.97 No 0.00 12.70 0.00 0.00N5990 Total 27.35 546.97 0.00 12.70 0.00 0.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0372002004 Kokosing Materials - Plant 521 (0372002004) P901 Stack 303873.49 4590756.5 27.57 551.38 No 0.00 0.00 5.65 10.180372002004 Kokosing Materials - Plant 521 (0372002004) P901 303873.49 4590756.50 27.57 551.38 No 0.00 0.00 0.06 0.100372002004 Total 27.57 551.38 0.00 0.00 5.71 10.29 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoA4074 IKO MONROE, INC NAT GAS/FUEL OIL BOILER 300200.00 4644200.00 28.54 570.83 0.00 0.00 0.00 0.00A4074 IKO MONROE, INC ASPHALT ROOFING LINE 300200.00 4644200.00 28.54 570.83 2.45 2.45 0.00 0.00A4074 IKO MONROE, INC ASPHALT ROOFING LINE 300200.00 4644200.00 28.54 570.83 2.45 2.45 0.00 0.00A4074 Total 28.54 570.83 4.91 4.91 0.00 0.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0362000009 Materion Brush Inc. (0362000009) B006 Pebbles Plant Boiler No. 1 314987.71 4595346.37 29.91 598.12 Yes 0.21 0.21 2.71 2.280362000009 Materion Brush Inc. (0362000009) B007 Pebbles Plant Boiler No. 2 314987.71 4595346.37 29.91 598.12 Yes 0.21 0.21 2.74 2.300362000009 Materion Brush Inc. (0362000009) B012 9-4 314987.71 4595346.37 29.91 598.12 Yes 0.16 0.16 2.04 1.710362000009 Materion Brush Inc. (0362000009) B013 9-5 314987.71 4595346.37 29.91 598.12 Yes 0.24 0.24 3.21 2.700362000009 Materion Brush Inc. (0362000009) B014 9-6 314987.71 4595346.37 29.91 598.12 Yes 0.22 0.22 2.90 2.440362000009 Materion Brush Inc. (0362000009) P010 1-1 314987.71 4595346.37 29.91 598.12 Yes 1.46 1.46 2.62 107.510362000009 Materion Brush Inc. (0362000009) P037 9-1 314987.71 4595346.37 29.91 598.12 Yes 0.29 0.29 3.03 1.820362000009 Materion Brush Inc. (0362000009) P043 9-1 314987.71 4595346.37 29.91 598.12 Yes 0.29 0.29 3.03 1.820362000009 Materion Brush Inc. (0362000009) P093 1-1 314987.71 4595346.37 29.91 598.12 Yes 0.22 0.22 5.30 3.180362000009 Materion Brush Inc. (0362000009) P033 42-1 314987.71 4595346.37 29.91 598.12 Yes 0.42 0.42 7.49 0.000362000009 Materion Brush Inc. (0362000009) P033 42-2 314987.71 4595346.37 29.91 598.12 Yes 0.41 0.41 7.27 0.000362000009 Materion Brush Inc. (0362000009) P033 42-3 314987.71 4595346.37 29.91 598.12 Yes 0.41 0.41 7.27 0.000362000009 Materion Brush Inc. (0362000009) P051 15-4 314987.71 4595346.37 29.91 598.12 Yes 0.08 0.08 13.56 0.000362000009 Materion Brush Inc. (0362000009) P063 48-1 314987.71 4595346.37 29.91 598.12 Yes 1.11 1.11 0.00 0.000362000009 Materion Brush Inc. (0362000009) P063 9-1 314987.71 4595346.37 29.91 598.12 Yes 1.11 1.11 0.00 0.000362000009 Materion Brush Inc. (0362000009) B001 314987.71 4595346.37 29.91 598.12 Yes 0.42 0.42 4.79 0.480362000009 Total 29.91 598.12 7.25 7.25 67.98 126.24 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0387029240 Bowling Green State Univ (0387029240) B012 B012 277137.92 4588445.23 32.51 650.28 No 0.00 0.00 3.40 2.430387029240 Bowling Green State Univ (0387029240) B013 B013 277137.92 4588445.23 32.51 650.28 No 0.00 0.00 4.11 1.860387029240 Bowling Green State Univ (0387029240) B014 B014 277137.92 4588445.23 32.51 650.28 No 0.00 0.00 4.90 1.940387029240 Total 32.51 650.28 0.00 0.00 12.41 6.23 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoN7012 MID-AMERICAN RECYCLERS, INC ROTARY KILN DRYER 307776.00 4645845.00 32.62 652.38 25.40 25.40 0.00 0.00N7012 Total 32.62 652.38 25.40 25.40 0.00 0.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoN5675 SPARTAN STEEL COATING HOT DIP GALVANIZING LINE - CLEANING SECTION 305095.00 4647120.00 32.75 655.03 0.44 0.44 0.00 0.00N5675 SPARTAN STEEL COATING HOT DIP GALVANIZING LINE - FURNACE EXHAUST 305095.00 4647120.00 32.75 655.03 1.21 1.21 48.16 20.03N5675 SPARTAN STEEL COATING EU-CLEANING AND EU-FURNACES 305095.00 4647120.00 32.75 655.03 3.02 3.02 0.00 0.00N5675 SPARTAN STEEL COATING 305095.00 4647120.00 32.75 655.03 0.00 0.36 7.84 6.59N5675 Total 32.75 655.03 4.68 5.04 56.00 26.61 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoN1810 MICHIGAN AGRICULTURAL COMMODITIES RGDRYERS 263500.00 4634500.00 35.25 704.98 5.95 5.95 4.92 0.00N1810 MICHIGAN AGRICULTURAL COMMODITIES EU-Grain 263500.00 4634500.00 35.25 704.98 41.32 41.32 0.00 0.00N1810 MICHIGAN AGRICULTURAL COMMODITIES RGDRYERS 263500.00 4634500.00 35.25 704.98 5.95 5.95 4.92 0.00N1810 MICHIGAN AGRICULTURAL COMMODITIES EU-Grain 263500.00 4634500.00 35.25 704.98 41.32 41.32 0.00 0.00N1810 Total 35.25 704.98 94.54 94.54 9.84 0.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoB4321 DTE ENERGY EUFLEX5501 312850.00 4647650.00 36.63 732.58 0.00 0.00 7.98 6.74B4321 THE DTE ELECTRIC COMPANY - FERMI ENERGY CENTER 312850.00 4647650.00 36.63 732.58 0.00 0.00 693.93 154.25B4321 Total 36.63 732.58 0.00 0.00 701.91 160.99 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoB1743 HOLNAM, INC Rotary Kilns 279800.00 4652300.00 38.52 770.31 0.57 0.57 0.00 6.30B1743 HOLCIM (US), INC FG-TRUCK LOADING 279800.00 4652300.00 38.52 770.31 5.61 5.61 0.00 6.30B1743 HOLCIM (US), INC 279800.00 4652300.00 38.52 770.31 8.32 8.32 0.00 6.30B1743 Total 38.52 770.31 14.49 14.50 0.00 18.90 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0362010127 Ottawa County Landfill Gas Power Station (0362010127) P002 Stack #2 330311.32 4598234.71 40.83 816.56 Yes 1.01 1.01 5.36 22.790362010127 Total 40.83 816.56 1.01 1.01 5.36 22.79 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0362010118 Port Clinton Landfill (0362010118) P901 Flare stack-No Builidng had to Forced Dimensions 331019.44 4598773.52 41.23 824.61 Yes 0.32 0.43 3.81 8.640362010118 Port Clinton Landfill (0362010118) F002 F001 331019.44 4598773.52 41.23 824.61 Yes 5.49 6.75 0.00 0.000362010118 Total 41.23 824.61 5.80 7.18 3.81 8.64 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0372000081 Carmeuse Lime Inc Millersville Operations (0372000081) P005 P005-#1KILN 308908.24 4577351.19 41.89 837.74 Yes 7.95 31.80 79.47 29.10

Page 318: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx CO0372000081 Carmeuse Lime Inc Millersville Operations (0372000081) P006 P006-#2KILN 308908.24 4577351.19 41.89 837.74 Yes 5.67 22.67 63.47 23.250372000081 Carmeuse Lime Inc Millersville Operations (0372000081) P901 #1&#3 L.O. 308908.24 4577351.19 41.89 837.74 Yes 4.47 5.93 0.00 0.000372000081 Carmeuse Lime Inc Millersville Operations (0372000081) P903 P011-M.HAND 308908.24 4577351.19 41.89 837.74 Yes 6.81 9.24 0.00 0.000372000081 Carmeuse Lime Inc Millersville Operations (0372000081) P005 308908.24 4577351.19 41.89 837.74 Yes 0.08 0.32 0.80 0.290372000081 Carmeuse Lime Inc Millersville Operations (0372000081) P006 308908.24 4577351.19 41.89 837.74 Yes 0.06 0.23 0.64 0.230372000081 Carmeuse Lime Inc Millersville Operations (0372000081) F001 F001-UNPAV 308908.24 4577351.19 41.89 837.74 Yes 0.19 1.04 0.00 0.000372000081 Carmeuse Lime Inc Millersville Operations (0372000081) F002 F002-INACT 308908.24 4577351.19 41.89 837.74 Yes 0.04 0.13 0.00 0.000372000081 Carmeuse Lime Inc Millersville Operations (0372000081) F004 F004-SecC&S 308908.24 4577351.19 41.89 837.74 Yes 0.21 0.84 0.00 0.000372000081 Carmeuse Lime Inc Millersville Operations (0372000081) P903 P903 Fugitive Emissions (formerly P011) 308908.24 4577351.19 41.89 837.74 Yes 0.43 0.59 0.00 0.000372000081 Total 41.89 837.74 25.90 72.79 144.39 52.88 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0372030241 AMP Fremont Energy Center (0372030241) P001 P001 Turbine Emissions Release 318916.45 4582958.22 41.85 837.08 Yes 39.71 39.71 60.43 26.810372030241 AMP Fremont Energy Center (0372030241) P002 P002 Turbine Emissions Release 318916.45 4582958.22 41.85 837.08 Yes 50.67 50.67 55.67 39.970372030241 AMP Fremont Energy Center (0372030241) P003 Cooling Tower emissions release. 318916.45 4582958.22 41.85 837.08 Yes 0.00 0.47 0.00 0.000372030241 Total 41.85 837.08 90.39 90.86 116.10 66.78 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoN3597 STONECO NEWPORT 314800.00 4653800.00 42.92 858.42 41.75 41.75 0.00 0.00N3597 Total 42.92 858.42 41.75 41.75 0.00 0.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0372030199 ABC Inoac Exterior Systems, LLC (0372030199) K004 S4-24-K004 320083.85 4581478.23 43.74 874.77 Yes 26.72 26.72 0.45 0.380372030199 ABC Inoac Exterior Systems, LLC (0372030199) K004 S4-08-K004 320083.85 4581478.23 43.74 874.77 Yes 26.72 26.72 0.45 0.380372030199 ABC Inoac Exterior Systems, LLC (0372030199) K007 Exit stack of the RTO 320083.85 4581478.23 43.74 874.77 Yes 0.03 0.03 2.54 2.190372030199 ABC Inoac Exterior Systems, LLC (0372030199) K004 S4-12-K004 320083.85 4581478.23 43.74 874.77 Yes 26.72 26.72 0.11 0.090372030199 ABC Inoac Exterior Systems, LLC (0372030199) K004 S4-13-K004 320083.85 4581478.23 43.74 874.77 Yes 26.72 26.72 0.11 0.090372030199 ABC Inoac Exterior Systems, LLC (0372030199) K004 S4-15-K004 320083.85 4581478.23 43.74 874.77 Yes 26.72 26.72 0.22 0.190372030199 ABC Inoac Exterior Systems, LLC (0372030199) K004 S4-32-K004 320083.85 4581478.23 43.74 874.77 Yes 26.72 26.72 0.22 0.190372030199 ABC Inoac Exterior Systems, LLC (0372030199) K004 S4-33-K004 320083.85 4581478.23 43.74 874.77 Yes 26.72 26.72 0.11 0.090372030199 ABC Inoac Exterior Systems, LLC (0372030199) K004 S4-34-K004 320083.85 4581478.23 43.74 874.77 Yes 26.72 26.72 0.11 0.090372030199 ABC Inoac Exterior Systems, LLC (0372030199) K004 S4-16-K004 320083.85 4581478.23 43.74 874.77 Yes 26.72 26.72 0.22 0.190372030199 ABC Inoac Exterior Systems, LLC (0372030199) K004 S4-21-K004 320083.85 4581478.23 43.74 874.77 Yes 26.72 26.72 0.11 0.090372030199 ABC Inoac Exterior Systems, LLC (0372030199) K004 S4-23-K004 320083.85 4581478.23 43.74 874.77 Yes 26.72 26.72 0.11 0.090372030199 Total 43.74 874.77 293.93 293.93 4.79 4.09 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0372030100 P.H. Glatfelter Co. - Fremont Facility (0372030100) B004 Boiler 3 Stack 320387.34 4581532.92 43.88 877.57 No 0.18 0.18 3.28 1.970372030100 P.H. Glatfelter Co. - Fremont Facility (0372030100) K002 Drying Oven #2 Vent 320387.34 4581532.92 43.88 877.57 No 0.75 0.75 2.14 1.280372030100 P.H. Glatfelter Co. - Fremont Facility (0372030100) K002 Drying Oven #1 Vent 320387.34 4581532.92 43.88 877.57 No 0.75 0.75 2.14 1.280372030100 P.H. Glatfelter Co. - Fremont Facility (0372030100) K002 Paper Coating Station #2 Vent 320387.34 4581532.92 43.88 877.57 No 1.50 1.50 4.27 2.560372030100 P.H. Glatfelter Co. - Fremont Facility (0372030100) P003 Color Compounding Area Stack Vent 320387.34 4581532.92 43.88 877.57 No 4.60 4.60 0.00 0.000372030100 P.H. Glatfelter Co. - Fremont Facility (0372030100) P901 Vent. Scrub 320387.34 4581532.92 43.88 877.57 No 0.32 0.32 0.00 0.000372030100 P.H. Glatfelter Co. - Fremont Facility (0372030100) P003 Color Compound Area Fugitive Vent 320387.34 4581532.92 43.88 877.57 No 0.45 0.45 0.00 0.000372030100 P.H. Glatfelter Co. - Fremont Facility (0372030100) P901 Fugitive losses from P901 320387.34 4581532.92 43.88 877.57 No 0.01 0.01 0.00 0.000372030100 Total 43.88 877.57 100.00 100.00 100.00 100.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0372030210 Style Crest Enterprises, Inc. (0372030210) P013 Mill #9 323218.14 4582265.41 45.10 901.92 Yes 0.57 1.59 0.00 0.000372030210 Style Crest Enterprises, Inc. (0372030210) P014 Mill #10 323218.14 4582265.41 45.10 901.92 Yes 0.57 1.59 0.00 0.000372030210 Style Crest Enterprises, Inc. (0372030210) P015 Mill #5 Exhaust 323218.14 4582265.41 45.10 901.92 Yes 0.47 1.31 0.00 0.000372030210 Style Crest Enterprises, Inc. (0372030210) P013 Fugitive Building Emissions 323218.14 4582265.41 45.10 901.92 Yes 0.01 0.02 0.00 0.000372030210 Style Crest Enterprises, Inc. (0372030210) P014 Fugitive Building Emissions 323218.14 4582265.41 45.10 901.92 Yes 0.01 0.02 0.00 0.000372030210 Style Crest Enterprises, Inc. (0372030210) P015 Fugitive Building Emissions 323218.14 4582265.41 45.10 901.92 Yes 0.00 0.01 0.00 0.000372030210 Total 45.10 901.92 1.63 4.54 0.00 0.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoN5241 GREAT LAKES AGGREGATES, L.L.C. - SYLVANIA MINERALS 312000.00 4658000.00 45.43 908.62 140.93 140.93 0.00 0.00N5241 Total 45.43 908.62 140.93 140.93 0.00 0.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoN5986 CARLETON FARMS LANDFILL EU_FLARE Enclosed LFG Flare used in active LFG control syst 299500.00 4662700.00 46.66 933.17 0.00 0.00 75.86 252.88N5986 CARLETON FARMS LANDFILL EU_OpenflareOpen LFG Flare used in active LFG control System 299500.00 4662700.00 46.66 933.17 0.00 0.00 171.52 604.13N5986 CARLETON FARMS LANDFILL RGPHASE2 299500.00 4662700.00 46.66 933.17 4.39 4.39 53.10 158.82N5986 CARLETON FARMS LANDFILL RGPHASE1 299500.00 4662700.00 46.66 933.17 6.14 6.14 50.83 212.25N5986 SUMPTER ENERGY ASSOCIATES REC. INTERNAL COMBUSTION ENGINES 299500.00 4662700.00 46.66 933.17 0.00 0.00 0.00 31.89N5986 CARLETON FARMS LANDFILL EU_HAULING 299500.00 4662700.00 46.66 933.17 58.24 58.24 0.00 0.00N5986 CARLETON FARMS LANDFILL RGPHASE2 299500.00 4662700.00 46.66 933.17 4.39 4.39 53.10 158.82N5986 CARLETON FARMS LANDFILL RGPHASE1 299500.00 4662700.00 46.66 933.17 6.14 6.14 50.83 212.25N5986 CARLETON FARMS LANDFILL EU_HAULING 299500.00 4662700.00 46.66 933.17 58.24 58.24 0.00 0.00N5986 Total 46.66 933.17 137.54 137.54 455.24 1631.04 N N N N NA NA NA NA Screen Screen Screen Model No No No Yes0372030070 The Kraft Heinz Company (0372030070) B006 EPB006 324902.61 4580773.66 47.33 946.53 Yes 0.03 0.03 1.07 0.320372030070 Total 47.33 946.53 0.03 0.03 1.07 0.32 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0326000076 WORTHINGTON STEEL (0326000076) B001 Pickle Line Boilers Stack 247120.16 4607312.75 47.50 950.05 No 0.00 0.00 0.00 0.000326000076 WORTHINGTON STEEL (0326000076) B002 Pickle Line Boilers Stack 247120.16 4607312.75 47.50 950.05 No 0.00 0.00 0.00 0.000326000076 WORTHINGTON STEEL (0326000076) P004 Galvanize Line Furnace Stack 247120.16 4607312.75 47.50 950.05 No 0.00 0.11 2.01 0.580326000076 WORTHINGTON STEEL (0326000076) P004 Galvanize Line Alkaline Cleaner Stack 247120.16 4607312.75 47.50 950.05 No 0.00 0.11 2.07 0.600326000076 WORTHINGTON STEEL (0326000076) P004 Galvanize Line Alkaline Cleaner Dryer Stack 247120.16 4607312.75 47.50 950.05 No 0.00 0.11 2.01 0.580326000076 WORTHINGTON STEEL (0326000076) P005 Galvanize Line Furnace Stack 247120.16 4607312.75 47.50 950.05 No 0.00 1.00 26.30 0.660326000076 WORTHINGTON STEEL (0326000076) P002 Pickle Line Fume Scrubber Stack 247120.16 4607312.75 47.50 950.05 No 0.00 0.18 0.00 0.000326000076 WORTHINGTON STEEL (0326000076) P008 Generator - Emergency Back-up - Galv 247120.16 4607312.75 47.50 950.05 No 0.00 0.00 0.00 0.000326000076 WORTHINGTON STEEL (0326000076) P009 Generator - Emergency Back-up - Galv 247120.16 4607312.75 47.50 950.05 No 0.00 0.00 0.00 0.000326000076 WORTHINGTON STEEL (0326000076) P002 Pickle Line Fume Scrubber - Fugitive Emissions 247120.16 4607312.75 47.50 950.05 No 0.00 0.01 0.00 0.000326000076 Total 47.50 950.05 100.00 100.00 100.00 100.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoA7757 U S SILICA CO EU-SANDDRY new wet scrubber stack 315500.00 4658500.00 47.39 947.81 15.34 0.00 8.79 7.39A7757 U S SILICA CO EU-HD01 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00A7757 U S SILICA CO EU-VF03 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00A7757 U S SILICA CO EU-VF01 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00A7757 U S SILICA CO EU-VF02 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00A7757 U S SILICA CO EU-BC02 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00A7757 U S SILICA CO EU-BC01 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00

Page 319: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx COA7757 U S SILICA CO EU-BC03 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00A7757 U S SILICA CO EU-BC06 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00A7757 U S SILICA CO EU-HS01 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00A7757 U S SILICA CO EU-RecHopper 315500.00 4658500.00 47.39 947.81 0.21 0.00 0.00 0.00A7757 U S SILICA CO EU-HD02 315500.00 4658500.00 47.39 947.81 0.25 0.00 0.00 0.00A7757 U S SILICA COMPANY SVCOLLECTORA 30.0 MM BTU/hr natural gas or propane fired fl 315500.00 4658500.00 47.39 947.81 20.19 20.19 0.00 0.00A7757 U S SILICA COMPANY SVWETSCRUBA 30.0 MM BTU/hr natural gas or propane fired fl 315500.00 4658500.00 47.39 947.81 0.00 30.70 0.00 0.00A7757 U S SILICA CO EU-HD01 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00A7757 U S SILICA CO EU-VF03 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00A7757 U S SILICA CO EU-VF01 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00A7757 U S SILICA CO EU-VF02 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00A7757 U S SILICA CO EU-BC02 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00A7757 U S SILICA CO EU-BC01 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00A7757 U S SILICA CO EU-BC03 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00A7757 U S SILICA CO EU-BC06 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00A7757 U S SILICA CO EU-HS01 315500.00 4658500.00 47.39 947.81 0.00 0.00 0.00 0.00A7757 U S SILICA CO EU-RecHopper 315500.00 4658500.00 47.39 947.81 0.21 0.00 0.00 0.00A7757 U S SILICA CO EU-HD02 315500.00 4658500.00 47.39 947.81 0.25 0.00 0.00 0.00A7757 Total 47.39 947.81 36.45 50.90 8.79 7.39 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoB1877 GUARDIAN INDUSTRIES Stack for Glass Manufacturing Line 1 Dust Collecti 304915.00 4662490.00 47.43 948.53 0.04 0.04 0.00 0.00B1877 GUARDIAN INDUSTRIES Oil Mist Eliminator for pumps used at G-49 Sputte 304915.00 4662490.00 47.43 948.53 0.08 0.08 0.00 0.00B1877 GUARDIAN INDUSTRIES glass edge sanding device dust collector 304915.00 4662490.00 47.43 948.53 0.83 0.83 0.00 0.00B1877 GUARDIAN INDUSTRIES Stack for Glass Manufacturing Line 2, dust collecti 304915.00 4662490.00 47.43 948.53 0.45 0.45 0.00 0.00B1877 GUARDIAN INDUSTRIES Emergency Generator 304915.00 4662490.00 47.43 948.53 151.58 151.58 2154.21 463.65B1877 GUARDIAN INDUSTRIES #1 Glass Production Line Stack 304915.00 4662490.00 47.43 948.53 120.67 120.67 589.98 6.35B1877 GUARDIAN INDUSTRIES #2 Glass Production Line Stack 304915.00 4662490.00 47.43 948.53 153.29 153.29 1294.61 8.07B1877 GUARDIAN INDUSTRIES glass edge sanding device dust collector 304915.00 4662490.00 47.43 948.53 0.83 0.83 0.00 0.00B1877 Total 47.43 948.53 427.76 427.76 4038.79 478.07 N N N N NA NA NA NA Screen Screen Model Screen No No Yes No0387000376 Charter Steel (0387000376) B002 BLR-04-01 297129.65 4568812.83 47.71 954.10 Yes 0.20 0.20 1.30 2.170387000376 Charter Steel (0387000376) P005 AF05-01 297129.65 4568812.83 47.71 954.10 Yes 0.04 0.04 0.44 0.450387000376 Charter Steel (0387000376) P005 AF05-02 297129.65 4568812.83 47.71 954.10 Yes 0.04 0.04 0.42 0.430387000376 Charter Steel (0387000376) P005 AF05-03 297129.65 4568812.83 47.71 954.10 Yes 0.04 0.04 0.42 0.430387000376 Charter Steel (0387000376) P006 AF06-01 297129.65 4568812.83 47.71 954.10 Yes 0.04 0.04 0.43 0.440387000376 Charter Steel (0387000376) P006 AF06-02 297129.65 4568812.83 47.71 954.10 Yes 0.04 0.04 0.45 0.450387000376 Charter Steel (0387000376) P006 AF06-03 297129.65 4568812.83 47.71 954.10 Yes 0.04 0.04 0.43 0.440387000376 Charter Steel (0387000376) P007 AF07-01 297129.65 4568812.83 47.71 954.10 Yes 0.04 0.04 0.44 0.460387000376 Charter Steel (0387000376) P007 AF07-02 297129.65 4568812.83 47.71 954.10 Yes 0.04 0.04 0.44 0.460387000376 Charter Steel (0387000376) P007 AF07-03 297129.65 4568812.83 47.71 954.10 Yes 0.04 0.04 0.45 0.470387000376 Charter Steel (0387000376) P008 AF08-01 297129.65 4568812.83 47.71 954.10 Yes 0.05 0.05 0.51 0.510387000376 Charter Steel (0387000376) P008 AF08-02 297129.65 4568812.83 47.71 954.10 Yes 0.05 0.05 0.50 0.500387000376 Charter Steel (0387000376) P008 AF08-03 297129.65 4568812.83 47.71 954.10 Yes 0.05 0.05 0.50 0.500387000376 Charter Steel (0387000376) P009 AF01-01 297129.65 4568812.83 47.71 954.10 Yes 0.05 0.05 0.58 0.560387000376 Charter Steel (0387000376) P009 AF01-02 297129.65 4568812.83 47.71 954.10 Yes 0.05 0.05 0.58 0.560387000376 Charter Steel (0387000376) P009 AF01-03 297129.65 4568812.83 47.71 954.10 Yes 0.06 0.06 0.60 0.570387000376 Charter Steel (0387000376) P010 AF02-01 297129.65 4568812.83 47.71 954.10 Yes 0.05 0.05 0.54 0.520387000376 Charter Steel (0387000376) P010 AF02-02 297129.65 4568812.83 47.71 954.10 Yes 0.05 0.05 0.54 0.520387000376 Charter Steel (0387000376) P010 AF02-03 297129.65 4568812.83 47.71 954.10 Yes 0.05 0.05 0.55 0.540387000376 Charter Steel (0387000376) P011 AF03-01 297129.65 4568812.83 47.71 954.10 Yes 0.05 0.05 0.48 0.460387000376 Charter Steel (0387000376) P011 AF03-02 297129.65 4568812.83 47.71 954.10 Yes 0.05 0.05 0.48 0.460387000376 Charter Steel (0387000376) P011 AF03-03 297129.65 4568812.83 47.71 954.10 Yes 0.05 0.05 0.49 0.480387000376 Charter Steel (0387000376) P012 AF04-01 297129.65 4568812.83 47.71 954.10 Yes 0.05 0.05 0.59 0.560387000376 Charter Steel (0387000376) P012 AF04-02 297129.65 4568812.83 47.71 954.10 Yes 0.05 0.05 0.57 0.550387000376 Charter Steel (0387000376) P012 AF04-03 297129.65 4568812.83 47.71 954.10 Yes 0.05 0.05 0.57 0.550387000376 Charter Steel (0387000376) P901 SB#1-01 297129.65 4568812.83 47.71 954.10 Yes 0.29 0.68 0.00 0.000387000376 Charter Steel (0387000376) P901 Fugitive 297129.65 4568812.83 47.71 954.10 Yes 0.00 0.01 0.00 0.000387000376 Total 47.71 954.10 1.60 2.00 13.29 14.03 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoB3111 RECKITT BENCKISER, INC EU-Tabs Process 314400.00 4659400.00 47.71 954.11 2.98 2.98 0.00 0.00B3111 Total 47.71 954.11 2.98 2.98 0.00 0.00 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0372030005 Rexam Beverage Can Company (0372030005) B001 EP34 322441.36 4578087.32 47.87 957.31 Yes 0.02 0.02 0.33 0.270372030005 Rexam Beverage Can Company (0372030005) B002 EP34 322441.36 4578087.32 47.87 957.31 Yes 0.02 0.02 0.33 0.270372030005 Rexam Beverage Can Company (0372030005) B003 EP47 322441.36 4578087.32 47.87 957.31 Yes 0.05 0.05 0.68 0.580372030005 Rexam Beverage Can Company (0372030005) B004 EP47 322441.36 4578087.32 47.87 957.31 Yes 0.05 0.05 0.68 0.580372030005 Rexam Beverage Can Company (0372030005) B005 EP33 322441.36 4578087.32 47.87 957.31 Yes 0.01 0.01 0.14 0.120372030005 Rexam Beverage Can Company (0372030005) B005 EP48 322441.36 4578087.32 47.87 957.31 Yes 0.01 0.01 0.14 0.120372030005 Rexam Beverage Can Company (0372030005) B005 EP52 322441.36 4578087.32 47.87 957.31 Yes 0.01 0.01 0.14 0.120372030005 Rexam Beverage Can Company (0372030005) B005 EP53 322441.36 4578087.32 47.87 957.31 Yes 0.01 0.01 0.14 0.120372030005 Rexam Beverage Can Company (0372030005) B005 EP54 322441.36 4578087.32 47.87 957.31 Yes 0.01 0.01 0.14 0.120372030005 Rexam Beverage Can Company (0372030005) K001 EP40 322441.36 4578087.32 47.87 957.31 Yes 0.70 0.70 0.73 0.620372030005 Rexam Beverage Can Company (0372030005) K001 EP41 322441.36 4578087.32 47.87 957.31 Yes 0.70 0.70 0.73 0.620372030005 Rexam Beverage Can Company (0372030005) K001 EP35 322441.36 4578087.32 47.87 957.31 Yes 0.28 0.28 0.29 0.250372030005 Rexam Beverage Can Company (0372030005) K001 EP36 322441.36 4578087.32 47.87 957.31 Yes 0.28 0.28 0.29 0.250372030005 Rexam Beverage Can Company (0372030005) K001 EP37 322441.36 4578087.32 47.87 957.31 Yes 0.28 0.28 0.29 0.250372030005 Rexam Beverage Can Company (0372030005) K001 EP38 322441.36 4578087.32 47.87 957.31 Yes 0.28 0.28 0.29 0.250372030005 Rexam Beverage Can Company (0372030005) K001 EP39 322441.36 4578087.32 47.87 957.31 Yes 0.28 0.28 0.29 0.250372030005 Rexam Beverage Can Company (0372030005) K002 EP42 322441.36 4578087.32 47.87 957.31 Yes 0.69 0.69 0.52 0.430372030005 Rexam Beverage Can Company (0372030005) K002 EP43 322441.36 4578087.32 47.87 957.31 Yes 0.69 0.69 0.52 0.430372030005 Rexam Beverage Can Company (0372030005) K002 EP35 322441.36 4578087.32 47.87 957.31 Yes 0.28 0.28 0.21 0.17

Page 320: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx CO0372030005 Rexam Beverage Can Company (0372030005) K002 EP36 322441.36 4578087.32 47.87 957.31 Yes 0.28 0.28 0.21 0.170372030005 Rexam Beverage Can Company (0372030005) K002 EP37 322441.36 4578087.32 47.87 957.31 Yes 0.28 0.28 0.21 0.170372030005 Rexam Beverage Can Company (0372030005) K002 EP38 322441.36 4578087.32 47.87 957.31 Yes 0.28 0.28 0.21 0.170372030005 Rexam Beverage Can Company (0372030005) K002 EP39 322441.36 4578087.32 47.87 957.31 Yes 0.28 0.28 0.21 0.170372030005 Rexam Beverage Can Company (0372030005) K003 EP44 322441.36 4578087.32 47.87 957.31 Yes 0.69 0.69 0.52 0.430372030005 Rexam Beverage Can Company (0372030005) K003 EP45 322441.36 4578087.32 47.87 957.31 Yes 0.69 0.69 0.52 0.430372030005 Rexam Beverage Can Company (0372030005) K003 EP55 322441.36 4578087.32 47.87 957.31 Yes 0.45 0.45 0.34 0.290372030005 Rexam Beverage Can Company (0372030005) K003 EP56 322441.36 4578087.32 47.87 957.31 Yes 0.45 0.45 0.34 0.290372030005 Rexam Beverage Can Company (0372030005) K003 EP57 322441.36 4578087.32 47.87 957.31 Yes 0.47 0.47 0.35 0.290372030005 Rexam Beverage Can Company (0372030005) K001 EP46 322441.36 4578087.32 47.87 957.31 Yes 0.63 0.63 0.66 0.550372030005 Rexam Beverage Can Company (0372030005) K001 EP49 322441.36 4578087.32 47.87 957.31 Yes 0.63 0.63 0.66 0.550372030005 Rexam Beverage Can Company (0372030005) K002 EP46 322441.36 4578087.32 47.87 957.31 Yes 0.62 0.62 0.46 0.390372030005 Rexam Beverage Can Company (0372030005) K002 EP49 322441.36 4578087.32 47.87 957.31 Yes 0.62 0.62 0.46 0.390372030005 Rexam Beverage Can Company (0372030005) K003 EP46 322441.36 4578087.32 47.87 957.31 Yes 0.62 0.62 0.46 0.390372030005 Rexam Beverage Can Company (0372030005) K003 EP49 322441.36 4578087.32 47.87 957.31 Yes 0.62 0.62 0.46 0.390372030005 Rexam Beverage Can Company (0372030005) K001 322441.36 4578087.32 47.87 957.31 Yes 0.14 0.14 0.15 0.120372030005 Rexam Beverage Can Company (0372030005) K002 322441.36 4578087.32 47.87 957.31 Yes 0.14 0.14 0.10 0.090372030005 Rexam Beverage Can Company (0372030005) K003 322441.36 4578087.32 47.87 957.31 Yes 0.14 0.14 0.10 0.090372030005 Total 47.87 957.31 12.68 12.68 13.32 11.18 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoM4510 CITY SAND & LANDFILL INC RG-ENGINES 293500.00 4664600.00 48.20 964.06 1.12 1.12 14.41 21.46M4510 CITY SAND & LANDFILL INC RG-ENGINES 293500.00 4664600.00 48.20 964.06 1.12 1.12 14.41 21.46M4510 Total 48.20 964.06 2.23 2.23 28.81 42.92 N N N N NA NA NA NA Screen Screen Screen Screen No No No No0326000073 NorthStar Bluescope Steel, LLC (0326000073) P001 EP-P001 ST1 246093.96 4605248.76 48.94 978.77 Yes 4.95 4.95 98.99 34.650326000073 NorthStar Bluescope Steel, LLC (0326000073) P001 EP-P001 ST2 246093.96 4605248.76 48.94 978.77 Yes 4.95 4.95 98.99 34.650326000073 NorthStar Bluescope Steel, LLC (0326000073) P002 EP-P002 ST1 246093.96 4605248.76 48.94 978.77 Yes 2.63 2.63 39.42 18.400326000073 NorthStar Bluescope Steel, LLC (0326000073) P004 EP-MSRF 246093.96 4605248.76 48.94 978.77 Yes 0.26 0.26 8.76 1.750326000073 NorthStar Bluescope Steel, LLC (0326000073) P005 EP-MSRF 246093.96 4605248.76 48.94 978.77 Yes 0.26 0.26 8.76 1.750326000073 NorthStar Bluescope Steel, LLC (0326000073) P006 EP-MSRF 246093.96 4605248.76 48.94 978.77 Yes 0.22 0.22 7.01 1.400326000073 NorthStar Bluescope Steel, LLC (0326000073) P008 EP-MSRF 246093.96 4605248.76 48.94 978.77 Yes 0.22 0.22 7.01 1.400326000073 NorthStar Bluescope Steel, LLC (0326000073) P009 EP-MSRF 246093.96 4605248.76 48.94 978.77 Yes 0.22 0.22 7.01 1.400326000073 NorthStar Bluescope Steel, LLC (0326000073) P016 EP-MSRF 246093.96 4605248.76 48.94 978.77 Yes 0.26 0.26 8.76 1.750326000073 NorthStar Bluescope Steel, LLC (0326000073) P901 EP-BH 1 246093.96 4605248.76 48.94 978.77 Yes 88.10 88.10 786.65 10347.750326000073 NorthStar Bluescope Steel, LLC (0326000073) P901 EP-BH 2 246093.96 4605248.76 48.94 978.77 Yes 88.10 88.10 786.65 10347.750326000073 NorthStar Bluescope Steel, LLC (0326000073) P901 EP-MSRF 246093.96 4605248.76 48.94 978.77 Yes 88.10 88.10 786.65 10347.750326000073 NorthStar Bluescope Steel, LLC (0326000073) P902 EP-BH 1 246093.96 4605248.76 48.94 978.77 Yes 0.00 0.00 0.00 0.000326000073 NorthStar Bluescope Steel, LLC (0326000073) P902 EP-BH 2 246093.96 4605248.76 48.94 978.77 Yes 0.00 0.00 0.00 0.000326000073 NorthStar Bluescope Steel, LLC (0326000073) P902 EP-MSRF 246093.96 4605248.76 48.94 978.77 Yes 0.00 0.00 0.00 0.000326000073 NorthStar Bluescope Steel, LLC (0326000073) P903 EP-BH 1 246093.96 4605248.76 48.94 978.77 Yes 0.00 0.00 0.00 0.000326000073 NorthStar Bluescope Steel, LLC (0326000073) P903 EP-BH 2 246093.96 4605248.76 48.94 978.77 Yes 0.00 0.00 0.00 0.000326000073 NorthStar Bluescope Steel, LLC (0326000073) P903 EP-MSRF 246093.96 4605248.76 48.94 978.77 Yes 0.00 0.00 0.00 0.000326000073 NorthStar Bluescope Steel, LLC (0326000073) F002 EP-F002 SLO 246093.96 4605248.76 48.94 978.77 Yes 0.82 0.82 0.00 0.000326000073 NorthStar Bluescope Steel, LLC (0326000073) F002 EP-F002 SSE 246093.96 4605248.76 48.94 978.77 Yes 0.82 0.82 0.00 0.000326000073 NorthStar Bluescope Steel, LLC (0326000073) F003 EP-F003 SLO 246093.96 4605248.76 48.94 978.77 Yes 0.82 0.82 0.00 0.000326000073 NorthStar Bluescope Steel, LLC (0326000073) F003 EP-F003 SSW 246093.96 4605248.76 48.94 978.77 Yes 0.82 0.82 0.00 0.000326000073 NorthStar Bluescope Steel, LLC (0326000073) P003 EP-HSMRF 246093.96 4605248.76 48.94 978.77 Yes 8.06 8.06 0.00 0.000326000073 NorthStar Bluescope Steel, LLC (0326000073) P901 246093.96 4605248.76 48.94 978.77 Yes 88.10 88.10 786.65 10347.750326000073 NorthStar Bluescope Steel, LLC (0326000073) P902 246093.96 4605248.76 48.94 978.77 Yes 0.00 0.00 0.00 0.000326000073 NorthStar Bluescope Steel, LLC (0326000073) P903 246093.96 4605248.76 48.94 978.77 Yes 0.00 0.00 0.00 0.000326000073 NorthStar Bluescope Steel, LLC (0326000073) F005 EP-ROADS 246093.96 4605248.76 48.94 978.77 Yes 0.36 1.97 0.00 0.000326000073 NorthStar Bluescope Steel, LLC (0326000073) P014 EP-CTLAM 246093.96 4605248.76 48.94 978.77 Yes 195.00 195.00 0.00 0.000326000073 NorthStar Bluescope Steel, LLC (0326000073) P015 EP-CTLAM 246093.96 4605248.76 48.94 978.77 Yes 10.77 10.77 43.06 234.330326000073 Total 48.94 978.77 583.84 585.45 3474.35 41722.48 N N N N NA NA NA NA Screen Screen Model Model No No Yes YesA6714 Georgia-Pacific Corrugated II LLC Boiler No. 3 - Cleaver Brooks 16.33 MMBtu/Hr. Al 278400.00 4663100.00 49.16 983.18 0.00 0.00 2.86 2.40A6714 Georgia-Pacific Corrugated II LLC Starch Silo Bin Vent 278400.00 4663100.00 49.16 983.18 7.79 7.79 2.81 2.36A6714 Georgia-Pacific Corrugated II LLC Scrap Paper Conveying System (3) Cyclones = 1 @ 278400.00 4663100.00 49.16 983.18 0.00 0.00 2.81 2.36A6714 Georgia-Pacific Corrugated II LLC Scrap Paper Conveying System (3) Cyclones = 1 @ 278400.00 4663100.00 49.16 983.18 0.00 0.00 2.81 2.36A6714 Total 49.16 983.18 7.79 7.79 11.28 9.48 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoK2688 B.O.P. FEDERAL CORRECTIONAL INSTITUTE 279050.00 4663500.00 49.34 986.83 21.72 21.72 324.70 73.28K2688 BOP FED CORRECTIONAL INSTIT BOILERS 279050.00 4663500.00 49.34 986.83 5.86 5.86 5.99 17.40K2688 B.O.P. FEDERAL CORRECTIONAL INSTITUTE 279050.00 4663500.00 49.34 986.83 21.72 21.72 324.70 73.28K2688 Total 49.34 986.83 49.30 49.30 655.39 163.96 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoA2849 WACKER CHEMICAL CORP EU00004 255600.00 4648000.00 49.54 990.72 0.00 0.00 0.55 0.47A2849 WACKER CHEMICAL CORP EU00005 255600.00 4648000.00 49.54 990.72 0.00 0.00 1.41 1.18A2849 WACKER CHEMICAL CORP EU00003 GAS/OIL BOILER: 0073-BO01 255600.00 4648000.00 49.54 990.72 0.00 0.00 1.11 0.93A2849 WACKER CHEMICAL CORP EU00002 GAS/OIL BOILER: 0073-BO01 255600.00 4648000.00 49.54 990.72 0.00 0.00 1.11 0.94A2849 WACKER CHEMICAL CORP EU00002 GAS/OIL BOILER: 0072-BO01 255600.00 4648000.00 49.54 990.72 0.00 0.00 1.11 0.94A2849 WACKER CHEMICAL CORP EU00001 GAS/OIL BOILER: 0071-BO01 255600.00 4648000.00 49.54 990.72 0.00 0.00 0.93 0.78A2849 WACKER CHEMICAL CORP EU00010 HOT OIL HEATER: 0051-BO01 255600.00 4648000.00 49.54 990.72 0.00 0.00 0.05 0.00A2849 WACKER CHEMICAL CORP EU00004 255600.00 4648000.00 49.54 990.72 0.00 0.00 0.55 0.47A2849 WACKER CHEMICAL CORP EU00005 255600.00 4648000.00 49.54 990.72 0.00 0.00 1.41 1.18A2849 Total 49.54 990.72 0.00 0.00 8.24 6.88 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoN2369 ADRIAN LANDFILL EUOPENFLAR Stack associated with utility flare 251300.00 4642135.00 49.64 992.78 0.00 0.00 1.23 2.81N2369 ADRIAN ENERGY ASSOICATES FLARE 251300.00 4642135.00 49.64 992.78 0.00 0.00 0.00 93.10N2369 ADRIAN ENERGY ASSOCIATES 3 RICE 251300.00 4642135.00 49.64 992.78 0.00 0.00 0.00 93.10N2369 ADRIAN LANDFILL EU_LANDFILL 251300.00 4642135.00 49.64 992.78 0.77 0.77 0.00 0.00N2369 ADRIAN ENERGY ASSOICATES FLARE 251300.00 4642135.00 49.64 992.78 0.00 0.00 0.00 93.10N2369 ADRIAN LANDFILL EU_LANDFILL 251300.00 4642135.00 49.64 992.78 0.77 0.77 0.00 0.00

Page 321: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Off-Site Source ScreeningPotential Emissions (ton/yr) Source Within SIA? PSD Screening (if within SIA) 20D Screening (if outside SIA) Model?

Facility ID Source Description Emu_ID DescriptionEasting (X)

(m)Northing (Y)

(m)

Distance from Cliffs

(D) (km) 20D (km)Title V

Source? PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM25 PM10 NOx CO PM2.5 PM10 NOx CON2369 Total 49.64 992.78 1.54 1.54 1.23 282.11 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoM4768 FLAT ROCK METAL INC EUSPACEHEATERS 310089.00 4663986.00 50.32 1006.33 0.00 0.00 0.05 0.04M4768 FLAT ROCK METAL INC RGBOILERS12 310089.00 4663986.00 50.32 1006.33 0.41 0.41 5.33 4.48M4768 FLAT ROCK METAL INC EUFINISHLINE1 310089.00 4663986.00 50.32 1006.33 0.00 0.00 0.17 0.00M4768 FLAT ROCK METAL INC EUFINISHLINE2 310089.00 4663986.00 50.32 1006.33 0.00 0.00 0.17 0.00M4768 FLAT ROCK METAL INC EUFINISHLINE3 310089.00 4663986.00 50.32 1006.33 0.00 0.00 0.17 0.00M4768 FLAT ROCK METAL INC EUROUGHLINE2 310089.00 4663986.00 50.32 1006.33 2.83 2.83 0.00 0.00M4768 FLAT ROCK METAL INC EUROUGHLINE1 310089.00 4663986.00 50.32 1006.33 3.22 3.22 0.00 0.00M4768 FLAT ROCK METAL, INC ROUGLINE#1 310089.00 4663986.00 50.32 1006.33 0.00 31.54 0.00 0.00M4768 FLAT ROCK METAL INC EUSPACEHEATERS 310089.00 4663986.00 50.32 1006.33 0.00 0.00 0.05 0.04M4768 FLAT ROCK METAL INC RGBOILERS12 310089.00 4663986.00 50.32 1006.33 0.41 0.41 5.33 4.48M4768 FLAT ROCK METAL INC EUFINISHLINE1 310089.00 4663986.00 50.32 1006.33 0.00 0.00 0.17 0.00M4768 FLAT ROCK METAL INC EUFINISHLINE2 310089.00 4663986.00 50.32 1006.33 0.00 0.00 0.17 0.00M4768 FLAT ROCK METAL INC EUFINISHLINE3 310089.00 4663986.00 50.32 1006.33 0.00 0.00 0.17 0.00M4768 FLAT ROCK METAL INC EUROUGHLINE2 310089.00 4663986.00 50.32 1006.33 2.83 2.83 0.00 0.00M4768 FLAT ROCK METAL INC EUROUGHLINE1 310089.00 4663986.00 50.32 1006.33 3.22 3.22 0.00 0.00M4768 Total 50.32 1006.33 12.91 44.45 11.78 9.04 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoN3631 GS Materials, LLC 253000.00 4646500.00 50.66 1013.19 0.00 5.43 77.11 16.60N3631 G S MATERIALS, LLC Non-Metallic Mineral Crusher 253000.00 4646500.00 50.66 1013.19 0.00 30.00 7.72 1.66N3631 GS Materials, LLC 253000.00 4646500.00 50.66 1013.19 0.00 5.43 77.11 16.60N3631 G S MATERIALS, LLC Non-Metallic Mineral Crusher 253000.00 4646500.00 50.66 1013.19 0.00 30.00 7.72 1.66N3631 Total 50.66 1013.19 0.00 70.85 169.66 36.52 N N N N NA NA NA NA Screen Screen Screen Screen No No No NoGrand Total 12441.50 18566.26 55707.20 64923.70

Notes:1. Q<20D Screening is based on total facility emissions.2. Included all sources with emissions > PSD significant rates within SIA.3. Also included all sources >100 TPY within 50km, but can use 20D screening.4. 100 TPY was used as PTE in screening for all non-Title V sources.5. PTE set to actuals if no permit limit found.

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Model ID Source Description Length (ft) Width (ft)

Square Root of Area (ft)

Structure Height/Vertical Dimension (ft)

Source Adjacent to Building?

Release Height (ft)

Initial Horizontal

Dimension sY

(ft)Initial Vertical

Dimension sZ (ft) ReferenceMTR_1 Boat Unloading 25.0 25.0 25.0 23.0 No 23.0 5.81 5.34 Notes 1, 2, & 3

MTR_2 Hopper to Conveyor Drop 25.0 25.0 25.0 9.8 No 9.8 5.81 2.29 Notes 1, 2, & 3

MTR_3 Conveyor to Stacker Drop 25.0 25.0 25.0 16.4 No 16.4 5.81 3.81 Notes 1, 2, & 3

MTR_4 Stacker to Hopper 25.0 25.0 25.0 29.3 No 29.3 5.81 6.81 Notes 1, 2, & 3

TR_2 Conveyor to Stacker Machine 25.0 25.0 25.0 55.1 No 55.1 5.81 12.81 Notes 1, 2, & 3

WE_1 Oxide Stockpile Wind Erosion 1328.4 141.0 432.8 52.5 No 52.5 100.66 12.20 Notes 1, 2, & 3

TR_3 Stacker to Stockpile 25.0 25.0 25.0 52.5 No 52.5 5.81 12.20 Notes 1, 2, & 3

TR_4 Oxide Reclaim using Bucket Wheel to Conveyor 25.0 25.0 25.0 52.5 No 52.5 5.81 12.20 Notes 1, 2, & 3

TR_5 Conveyor from Reclaim Machine to Main Conveyor 25.0 25.0 25.0 13.6 No 13.6 5.81 3.17 Notes 1, 2, & 3

TR_8 Oxide Lumps Conveyor Transfer to Stockpile 131.2 49.2 80.3 125.3 Yes 62.7 18.68 29.14 Notes 1, 2, & 4

WE_2 Oxide Lumps Stockpile Wind Erosion 131.2 49.2 80.3 125.3 Yes 62.7 18.68 29.15 Notes 1, 2, & 4

FEL_1 FEL for Lump Reclaim Fugitive on Unpaved 131.2 49.2 80.3 125.3 Yes 62.7 18.68 29.15 Notes 1, 2, & 4

TR_9 Oxide Lumps Drop from FEL to Truck 131.2 49.2 80.3 125.3 Yes 62.7 18.68 29.15 Notes 1, 2, & 4

TR_11 Oxide Fines to Stockpile 25.0 25.0 25.0 21.3 No 21.3 5.81 4.96 Notes 1, 2, & 3

WE_3 Oxide Fines Stockpile Wind Erosion 25.0 25.0 25.0 21.3 No 21.3 5.81 4.96 Notes 1, 2, & 3

FEL_2 FEL for Oxides Fine Reclaim Fugitives on Unpaved 25.0 25.0 25.0 21.3 No 21.3 5.81 4.96 Notes 1, 2, & 3

TR_12 Oxide Fines from FEL to Truck 25.0 25.0 25.0 9.8 No 9.8 5.81 2.29 Notes 1, 2, & 3

TR_15 REMET Drop to Stockpile 25.0 25.0 25.0 10.5 No 10.5 5.81 2.43 Notes 1, 2, & 3

WE_4 REMET Stockpile Wind Erosion 25.0 25.0 25.0 10.5 No 10.5 5.81 2.43 Notes 1, 2, & 3

TR_16 REMET Transfer from FEL to Hopper 131.2 49.2 80.3 125.3 Yes 62.7 18.68 29.14 Notes 1, 2, & 4

TR-19 HBI Transfer from Conveyor to Stacker 25.0 25.0 25.0 42.1 No 42.1 5.81 9.80 Notes 1, 2, & 3

TR_20 HBI Transfer from Stacker to Stockpile 25.0 25.0 25.0 19.7 No 19.7 5.81 4.58 Notes 1, 2, & 3

WE_5 HBI Stockpile Wind Erosion 951.2 82.0 279.3 19.7 No 19.7 64.95 4.58 Notes 1, 2, & 3

FEL_4 HBI Reclaim FEL fugitives 25.0 25.0 25.0 3.3 No 3.3 5.81 0.76 Notes 1, 2, & 3

TR_21a HBI Reclaim Bucket Wheel to Conveyor 25.0 25.0 25.0 19.7 No 19.7 5.81 4.58 Notes 1, 2, & 3

TR_21b HBI Conveyor from Reclaim to Enclosed Conveyor 25.0 25.0 25.0 12.6 No 12.6 5.81 2.94 Notes 1, 2, & 3

TR-21c HBI Drop from FEL to Hopper 25.0 25.0 25.0 6.6 No 6.6 5.81 1.53 Notes 1, 2, & 3

TR_22 HBI Drop from Hopper to Conveyor 25.0 25.0 25.0 6.6 No 6.6 5.81 1.53 Notes 1, 2, & 3

TR_26 HBI Loadout Rail Enclosure 78.7 42.6 57.9 11.2 Yes 5.6 13.47 2.60 Notes 1, 2, & 4

TR_27 HBI Loadout Truck Enclosure 78.7 42.6 57.9 110.0 Yes 55.0 13.47 25.58 Notes 1, 2, & 4

TR_29 Feed Recovery Transfer to Stockpile 85.3 55.8 69.0 86.4 Yes 43.2 16.04 20.09 Notes 1, 2, & 4

WE_6 Feed Recovery Stockpile Wind Erosion 85.3 55.8 69.0 86.4 Yes 43.2 16.04 20.09 Notes 1, 2, & 4

FEL_5 Feed Recovery FEL Fugitive 85.3 55.8 69.0 86.4 Yes 43.2 16.04 20.09 Notes 1, 2, & 4

TR_30 Feed Recovery FEL to Hopper 85.3 55.8 69.0 86.4 Yes 43.2 16.04 20.09 Notes 1, 2, & 4

FEL_6 Product Oversize FEL Fugitive 85.3 55.8 69.0 86.4 Yes 43.2 16.04 20.09 Notes 1, 2, & 5

TR_31 Product Oversize FEL to Hopper 85.3 55.8 69.0 86.4 Yes 43.2 16.04 20.09 Notes 1, 2, & 6

Iron Units Non-Road Volume Source Parameter CalculationSource Dimensions Initial Dispersion Coefficients

Note 1: Release height of elevated source if not on or adjacent to building. One half structure height for source located on or adjacent to building. Truck and rail enclosure emissions assume to occur at top of enclosure..Note 2: Sigma Y value calculated as the square root of the area of release (length of side) divided by 4.3 (Table 3-1 of AERMOD Manual for single volume source).Note 3: Sigma Z value for elevated source not on or adjacent to a building calculated as the vertical dimension of source divided by 4.3.Note 4. Sigma Z value for elevated source on or adjacent (within 5L) to a building calculated based on the building/structure height divided by 2.15.

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Step 1: Adjusted Width of RoadRoad Width (ft) of 25 + 20 ft (6 m) = 45 ft

Step 2: Height of VolumeVehicle height (ft) of 15 X 1.7 = 25.5 ft

Step 3: Initial Sigma Y (Horizontal Dimension)Adjusted road width (ft) of 45 / 2.15 = 21.0 ft

Step 4: Initial Sigma Z (Vertical Dimension)Height of volume (ft) of 25.5 / 2.15 = 11.9 ft

Step 5: Height of ReleaseHeight of volume (ft) of 25.5 / 2 = 12.8 ft

Iron Units Roadway Volume Source Parameter Calculation

Page 324: Application for Revisions to the Prevention of Significant … · 2019-10-16 · This PTI revision application addresses PSD requirements as noted in . Table 4-1. Table 4-1. PSD Requirements

Iron Units Land Use Analysis Results

2006 NLCD Description

2006 NLCD

CategoryCell

Count #Total Area (km2) (30mx30m/cell)

Fraction Total Area Auer Land Use Description

Auer Code

Rural/Urban Selection

Open Water 11 3311 2.98 0.11 Water Surface A5 RuralPerennial Ice/Snow 12 0 0.00 0.00 Water Surfaces A5 RuralDeveloped, Open Space 21 4810 4.33 0.15 Metropolitan Natural A1 Rural

Estate Residential R4 RuralDeveloped, Low Intensity 22 8734 7.86 0.28 Common Residential R1 RuralDeveloped, Med Intensity 23 5848 5.26 0.19 Compact Residential R2 UrbanDeveloped, High Intensity 24 3390 3.05 0.11 Commercial C1 Urban

Heavy Industrial I1 UrbanLight - Moderate Industrial I2 UrbanCompact Residential R3 Urban

Barren Land 31 97 0.09 0.00 -- -- RuralDeciduous Forest 41 300 0.27 0.01 Undeveloped Rural A4 RuralEvergreen Forest 42 0 0.00 0.00 Undeveloped Rural A4 RuralMixed Forest 43 0 0.00 0.00 Undeveloped Rural A4 RuralDwarf Scrub 51 0 0.00 0.00 Undeveloped A3 RuralShrub/Scrub 52 0 0.00 0.00 Undeveloped A3 RuralGrassland/Herbaceous 71 190 0.17 0.01 Undeveloped A3 RuralSedge/Herbaceous 72 0 0.00 0.00 Undeveloped A3 RuralLichens 73 0 0.00 0.00 Undeveloped A3 RuralMoss 74 0 0.00 0.00 Undeveloped A3 RuralPasture/Hay 81 0 0.00 0.00 Agricultural Rural A2 RuralCultivated Crops 82 2562 2.31 0.08 Agricultural Rural A2 RuralWoody Wetlands 90 12 0.01 0.00 Undeveloped A3 Rural

Undeveloped Rural A4 RuralWater Surfaces A5 Rural

Emergent Herb Wetlands 95 2030 1.83 0.06 Undeveloped A3 RuralWater Surfaces A5 Rural

No Data -9999 0 0.00 0.00 -- -- --Total Area Urban 8.31 30% Urban

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For Additional Information or Questions, Contact Melanie Pitrolo (828) 257-4213 or [email protected]

Request for Applicability of Class I Area Modeling Analysis

Facility Name (Company Name) IronUnits LLC

New Facility or Modification? New Facility

Source Type/BART Applicability New Major Stationary Source under PSD

Project Location (County/State/ Lat. & Long. in decimal degrees) Lucas County, Ohio (41.674, -83.479)

Application Contacts

Applicant Consultant Air Agency Permit Engineer

Company IronUnits, LLC Company RTP Environmental Agency OEPA

Contact Jason Aagenes Contact David Keen Contact Christopher Beekman

Address Cliffs Natural Resources P.O. Box 180 Eveleth, MN 55734

Address

304A West Millbrook Rd Raleigh, NC 27609

Address Ohio Environmental Protection Agency,50 West Town Street, Suite 700, Columbus, OH 43215

Phone # (218) 744-6037 Phone # (919) 845-1422 x41 Phone # (614) 644-3597

Email [email protected] Email [email protected] Email [email protected]

Briefly Describe the Proposed Project

IronUnits, LLC (“IU”) is seeking authorization in the form of a PSD Permit to Install for a proposed Hot Briquetted Iron (“HBI”)/Direct Reduced Iron (“DRI”) manufacturing facility at the Ironville brownfield site in Toledo, Lucas County, Ohio identified as the “HBI facility” or “Project”. The HBI Project will utilize the MIDREX process to produce up to 2.48 million tons per year of HBI or DRI from low-silica taconite pellets. The HBI Project will be situated on a brownfield parcel known as Ironville located on the southwest corner of Millard Ave and Front Street. The HBI Facility will use lake vessels, trains, and trucks to transport various raw-materials and products to and from the site.

Proposed Emissions and BACT

Criteria Pollutant

Emissions Emission Factor

(AP-42, Stack Test, Other?)

Proposed BACT Maximum hourly (lb/hr)

Proposed Annual (tons/yr)

Nitrogen Oxides 108.6 464.4 Equipment specs Use of low-NOx Burners

Sulfur Dioxide 4.8 21.0 Equipment specs NA – not applicable as not subject to PSD for SO2.

Particulate Matter 31.7 124.34 Equipment specs Use of baghouses, venturi scrubbers and fugitive emissions controls

Sulfuric Acid Mist 0 0 NA NA

Proximity to Class I Areas

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Class I Area Otter Creek

Distance from Facility (km) 436

.

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For Additional Information or Questions, Contact Melanie Pitrolo (828) 257-4213 or [email protected]

Figure 1. Location of the Proposed IU in Lucas County and the Closest Class I Area

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1

David Keen

From: Pitrolo, Melanie -FS <[email protected]>Sent: Monday, August 14, 2017 4:55 PMTo: David KeenSubject: RE: Request for Applicability of Class I Area Modeling Analysis

Hi David.  Thanks for sending information regarding the PSD application for IronUnits LLC.  Based on the information submitted, it is not anticipated that emissions from the project will cause or contribute to any adverse impacts of Air Quality Related Values (AQRVs) at Class I Areas managed by the USDA Forest Service.  Therefore, we will not be requesting that an AQRV modeling analysis be included as part of the application.    Thanks, Melanie    

Melanie Pitrolo Air Quality Specialist Forest Service Region 8, National Forests in North Carolina p: 828-257-4213 f: 828-257-4874 [email protected] 160 Zillicoa Street, Suite A Asheville, NC 28801 www.fs.fed.us

Caring for the land and serving people

 

    

From: David Keen [mailto:keen@rtpenv‐nc.com]  Sent: Tuesday, August 08, 2017 9:12 AM To: Pitrolo, Melanie ‐FS <[email protected]> Cc: Aagenes, Jason D <[email protected]>; Gurinder (Gary) Saini <saini@rtpenv‐nc.com>; Chris Beekman ([email protected]) <[email protected]>; David Keen ([email protected]) <[email protected]> Subject: Request for Applicability of Class I Area Modeling Analysis  Melanie, IronUnits LLC is proposing to construct a Hot Briquetted Iron (HBI)/ Direct Reduced Iron (DRI) manufacturing facility at the Ironville brownfield site in Toledo, Ohio (Lucas County). Please find attached our "Request for Applicability of Class I Area Modeling". Should you have any questions about our request or need additional information, please do not hesitate to contact me at (919) 845-1422 x41. Please let me know when you have successfully received this request.

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Thank you very much, David Keen    __________________ David Keen RTP Environmental [email protected] (919) 845-1422 x41 (919) 845-1424 fax (919) 906-6016 mobile Note: This message originates from RTP Environmental Associates Inc. It contains information that may be confidential or privileged and is intended only for the individual or entity named above. It is prohibited for anyone else to disclose, copy, distribute, or use the contents of this message. All personal messages express views solely of the sender, which are not to be attributed to RTP Environmental, and may not be copied or distributed without this disclaimer. If you received this message in error, please notify me immediately at: [email protected] or 919-845-1422 x41.     This electronic message contains information generated by the USDA solely for the intended recipients. Any unauthorized interception of this message or the use or disclosure of the information it contains may violate the law and subject the violator to civil or criminal penalties. If you believe you have received this message in error, please notify the sender and delete the email immediately.  

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IronUnits LLC

ATTACHMENT B MODEL SUMMARY RESULTS

AERMOD RESULTS

MERPS CALCULATIONS VISCREEN RESULTS

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Iron Units HBI Significant Impact, MAGLC, and 1-hr NO2 Increment Analysis - Post Application Analysis (9-11-19)Model File Pollutant Average Group Rank Conc/Dep East (X) North (Y) Elev Hill Flag Time Met File Sources Groups ReceptorsAERMOD 18081 IronUnits SIL & MAGLC_2013_CO.SUM CO 1-HR ALL 1ST 3010.342 294169.9 4616360.1 178.31 188.98 0 13041616 KTDZ_KDTX_2013.SFC 7 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2014_CO.SUM CO 1-HR ALL 1ST 2926.661 294128.6 4616421.2 176.62 187.32 0 14061610 KTDZ_KDTX_2014.SFC 7 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2015_CO.SUM CO 1-HR ALL 1ST 2922.251 294183.7 4616339.7 178.97 189.12 0 15082611 KTDZ_KDTX_2015.SFC 7 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2017_CO.SUM CO 1-HR ALL 1ST 2874.804 294211.3 4616298.9 179.85 189.12 0 17061311 KTDZ_KDTX_2017.SFC 7 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2016_CO.SUM CO 1-HR ALL 1ST 2831.45 294183.7 4616339.7 178.97 189.12 0 16100213 KTDZ_KDTX_2016.SFC 7 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2013_CO.SUM CO 8-HR ALL 1ST 1744.428 294235.5 4616278 179.99 189.12 0 13061116 KTDZ_KDTX_2013.SFC 7 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2015_CO.SUM CO 8-HR ALL 1ST 1645.456 294060.9 4615974.8 180.25 180.25 0 15032716 KTDZ_KDTX_2015.SFC 7 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2016_CO.SUM CO 8-HR ALL 1ST 1627.868 294183.7 4616339.7 178.97 189.12 0 16100216 KTDZ_KDTX_2016.SFC 7 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2017_CO.SUM CO 8-HR ALL 1ST 1556.153 294128.6 4616421.2 176.62 187.32 0 17062516 KTDZ_KDTX_2017.SFC 7 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2014_CO.SUM CO 8-HR ALL 1ST 1538.35 293743.5 4616672 179.69 179.69 0 14101316 KTDZ_KDTX_2014.SFC 7 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2014_HEXANE.SUM HEXANE 1-HR ALL 1ST 0.07845 291100 4617200 179.54 179.54 0 14021212 KTDZ_KDTX_2014.SFC 1 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2017_HEXANE.SUM HEXANE 1-HR ALL 1ST 0.05588 294800 4619100 173.26 173.26 0 17011514 KTDZ_KDTX_2017.SFC 1 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2015_HEXANE.SUM HEXANE 1-HR ALL 1ST 0.05417 291000 4615500 177.06 177.06 0 15033108 KTDZ_KDTX_2015.SFC 1 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2016_HEXANE.SUM HEXANE 1-HR ALL 1ST 0.05138 293150 4617000 177.03 177.03 0 16081018 KTDZ_KDTX_2016.SFC 1 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2013_HEXANE.SUM HEXANE 1-HR ALL 1ST 0.04785 290800 4617600 180.72 180.72 0 13020913 KTDZ_KDTX_2013.SFC 1 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2017_NH3.SUM NH3 1-HR ALL 1ST 261.4008 293709.6 4616705.7 179.7 179.7 0 17073122 KTDZ_KDTX_2017.SFC 2 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2014_NH3.SUM NH3 1-HR ALL 1ST 244.2463 293709.6 4616705.7 179.7 179.7 0 14072205 KTDZ_KDTX_2014.SFC 2 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2015_NH3.SUM NH3 1-HR ALL 1ST 207.4929 293705.3 4616705.7 179.82 179.82 0 15082806 KTDZ_KDTX_2015.SFC 2 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2016_NH3.SUM NH3 1-HR ALL 1ST 172.5934 293692.2 4616718.8 179.8 179.8 0 16041806 KTDZ_KDTX_2016.SFC 2 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2013_NH3.SUM NH3 1-HR ALL 1ST 97.87506 293726.5 4616688.9 179.66 179.66 0 13061207 KTDZ_KDTX_2013.SFC 2 1 8362AERMOD 18081 IronUnits SIL & MAGLC_5yrs_NO2.SUM NO2 1ST-HIGHEST MAX DAILY 1-HR ALL 1ST 14.47116 293777.4 4616638.3 179.75 179.75 0 5 YEARS KTDZ_KDTX_2013_2017.SFC 5 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2014_NOX.SUM NOX 1-HR ALL 1ST 38.86588 293800 4616800 179.72 179.72 0 14011711 KTDZ_KDTX_2014.SFC 9 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2016_NOX.SUM NOX 1-HR ALL 1ST 38.37297 293850 4616850 179.75 179.75 0 16050224 KTDZ_KDTX_2016.SFC 9 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2015_NOX.SUM NOX 1-HR ALL 1ST 37.30119 293642 4616079.6 180.4 180.4 0 15072701 KTDZ_KDTX_2015.SFC 9 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2017_NOX.SUM NOX 1-HR ALL 1ST 35.67621 293622.3 4616094.2 180.35 180.35 0 17070604 KTDZ_KDTX_2017.SFC 9 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2013_NOX.SUM NOX 1-HR ALL 1ST 21.25397 293661.7 4616065.1 179.9 179.9 0 13120204 KTDZ_KDTX_2013.SFC 9 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2014_NOX.SUM NOX ANNUAL ALL 1ST 1.2533 293883.8 4616620.7 179.33 179.33 0 1 YEARS KTDZ_KDTX_2014.SFC 9 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2015_NOX.SUM NOX ANNUAL ALL 1ST 1.24512 293906.1 4616620.5 179.22 179.22 0 1 YEARS KTDZ_KDTX_2015.SFC 9 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2017_NOX.SUM NOX ANNUAL ALL 1ST 1.15979 293928.5 4616620.2 179.25 179.25 0 1 YEARS KTDZ_KDTX_2017.SFC 9 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2016_NOX.SUM NOX ANNUAL ALL 1ST 1.13998 293969.2 4616591 179.14 179.14 0 1 YEARS KTDZ_KDTX_2016.SFC 9 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2013_NOX.SUM NOX ANNUAL ALL 1ST 1.09675 293906.1 4616620.5 179.22 179.22 0 1 YEARS KTDZ_KDTX_2013.SFC 9 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2016_PM10.SUM PM10 24-HR ALL 1ST 27.14614 293407.6 4616618.5 179.63 179.63 0 16010724 KTDZ_KDTX_2016.SFC 148 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2014_PM10.SUM PM10 24-HR ALL 1ST 25.69084 293430.3 4616650.7 179.52 179.52 0 14122024 KTDZ_KDTX_2014.SFC 148 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2017_PM10.SUM PM10 24-HR ALL 1ST 22.67121 293393.9 4616597.9 179.5 179.5 0 17091624 KTDZ_KDTX_2017.SFC 148 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2015_PM10.SUM PM10 24-HR ALL 1ST 20.09789 294003.8 4616567.3 178.9 178.9 0 15022724 KTDZ_KDTX_2015.SFC 148 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2013_PM10.SUM PM10 24-HR ALL 1ST 17.48011 293582.9 4616123.2 180.59 180.59 0 13011524 KTDZ_KDTX_2013.SFC 148 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2015_PM-10.SUM PM-10 ANNUAL ALL 1ST 2.52868 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2015.SFC 156 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2016_PM-10.SUM PM-10 ANNUAL ALL 1ST 2.2554 293200 4617050 176.94 176.94 0 1 YEARS KTDZ_KDTX_2016.SFC 156 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2014_PM-10.SUM PM-10 ANNUAL ALL 1ST 2.25 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2014.SFC 156 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2017_PM-10.SUM PM-10 ANNUAL ALL 1ST 2.24494 293200 4617050 176.94 176.94 0 1 YEARS KTDZ_KDTX_2017.SFC 156 1 8362AERMOD 18081 IronUnits SIL & MAGLC_2013_PM-10.SUM PM-10 ANNUAL ALL 1ST 2.07724 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2013.SFC 156 1 8362AERMOD 18081 IronUnits SIL & MAGLC_5yrs_PM25.SUM PM25 1ST-HIGHEST 24-HR ALL 1ST 6.96268 293582.9 4616123.2 180.59 180.59 0 5 YEARS KTDZ_KDTX_2013_2017.SFC 148 1 8362AERMOD 18081 IronUnits SIL & MAGLC_5yrs_PM-25.SUM PM-25 ANNUAL ALL 1ST 0.97017 294003.8 4616567.3 178.9 178.9 0 5 YEARS KTDZ_KDTX_2013_2017.SFC 156 1 8362

Iron Units HBI Significant Impact, MAGLC, and 1-hr NO2 Increment Analysis - Post Application Analysis (9-11-19)

Pollutant Average Group Rank

Model Conc.

(ug/m3)

Secondary PM25

(ug/m3)Total

(ug/m3)Standard (ug/m3) % Standard Analysis SIA (km)

NO2 1ST-HIGHEST MAX DAILY 1-HR ALL 1ST 14.47 NA 14.5 7.5 193% Significance 1.6NOx ANNUAL ALL 1ST 1.25 NA 1.3 1.0 125% Significance 0.59NOx 1-HR ALL 1ST 38.87 NA 38.9 188.0 21% State Increment NA

CO 1-HR ALL 1ST 3010.34 NA 3010.3 2000.0 151% Significance 0.82CO 8-HR ALL 1ST 1744.43 NA 1744.4 500.0 349% Significance 2.5

PM10 24-HR ALL 1ST 27.15 NA 27.1 5.0 543% Significance 2.2PM-10 ANNUAL ALL 1ST 2.53 NA 2.5 1.0 253% Significance 0.9

PM25 1ST-HIGHEST 24-HR ALL 1ST 6.96 0.070 7.03 1.2 586% Significance 2.9PM-25 ANNUAL ALL 1ST 0.97 0.002 0.97 0.2 486% Significance 1.6

NH3 1-HR ALL 1ST 261.40 NA 261.4 415 63% MAGLC NAHexane 1-HR ALL 1ST 0.08 NA 0.1 4,196 0.0019% MAGLC NA1-hr NOx->NO2 conversion assumes ARM2 with min and max ratios of 0.5 and 0.9, respectively. 100% conversion assumed for 1-hr state increment and annual average. Intermittent emissions from emergency generator and flaring events excluded from short-term averages (i.e., 1 through 24 hour).Secondary PM2.5 formation included.NA - Not applicable.

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Iron Units HBI NAAQS Analysis (9-13-19)Model File Pollutant Average Group Rank Conc/Dep East (X) North (Y) Elev Hill Flag Time Met File Sources Groups ReceptorsAERMOD 18081 IronUnits NAAQS_2013_CO.SUM CO 1-HR ALL 2ND 2844.888 294128.6 4616421.2 176.62 187.32 0 13102512 KTDZ_KDTX_2013.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2015_CO.SUM CO 1-HR ALL 2ND 2814.621 294197.5 4616319.3 179.47 189.12 0 15060910 KTDZ_KDTX_2015.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2017_CO.SUM CO 1-HR ALL 2ND 2800.985 294142.3 4616400.8 176.94 188.32 0 17090310 KTDZ_KDTX_2017.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2014_CO.SUM CO 1-HR ALL 2ND 2771.807 294128.6 4616421.2 176.62 187.32 0 14061609 KTDZ_KDTX_2014.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2016_CO.SUM CO 1-HR ALL 2ND 2705.277 294197.5 4616319.3 179.47 189.12 0 16070908 KTDZ_KDTX_2016.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2013_CO.SUM CO 1-HR CLIFFS 2ND 2842.274 294128.6 4616421.2 176.62 187.32 0 13102512 KTDZ_KDTX_2013.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2015_CO.SUM CO 1-HR CLIFFS 2ND 2814.225 294197.5 4616319.3 179.47 189.12 0 15060910 KTDZ_KDTX_2015.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2017_CO.SUM CO 1-HR CLIFFS 2ND 2799.535 294142.3 4616400.8 176.94 188.32 0 17090310 KTDZ_KDTX_2017.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2014_CO.SUM CO 1-HR CLIFFS 2ND 2769.811 294128.6 4616421.2 176.62 187.32 0 14061609 KTDZ_KDTX_2014.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2016_CO.SUM CO 1-HR CLIFFS 2ND 2704.933 294197.5 4616319.3 179.47 189.12 0 16070908 KTDZ_KDTX_2016.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2013_CO.SUM CO 1-HR LT20K 2ND 2844.216 294128.6 4616421.2 176.62 187.32 0 13102512 KTDZ_KDTX_2013.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2015_CO.SUM CO 1-HR LT20K 2ND 2814.45 294197.5 4616319.3 179.47 189.12 0 15060910 KTDZ_KDTX_2015.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2017_CO.SUM CO 1-HR LT20K 2ND 2800.772 294142.3 4616400.8 176.94 188.32 0 17090310 KTDZ_KDTX_2017.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2014_CO.SUM CO 1-HR LT20K 2ND 2771.085 294128.6 4616421.2 176.62 187.32 0 14061609 KTDZ_KDTX_2014.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2016_CO.SUM CO 1-HR LT20K 2ND 2705.147 294197.5 4616319.3 179.47 189.12 0 16070908 KTDZ_KDTX_2016.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2014_CO.SUM CO 8-HR ALL 2ND 1429.301 293760.4 4616655.2 179.58 179.58 0 14122608 KTDZ_KDTX_2014.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2015_CO.SUM CO 8-HR ALL 2ND 1412.052 294183.7 4616339.7 178.97 189.12 0 15082616 KTDZ_KDTX_2015.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2017_CO.SUM CO 8-HR ALL 2ND 1374.33 294156.1 4616380.5 177.5 188.85 0 17090716 KTDZ_KDTX_2017.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2013_CO.SUM CO 8-HR ALL 2ND 1319.797 294114.8 4616441.6 176.57 185.8 0 13032108 KTDZ_KDTX_2013.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2016_CO.SUM CO 8-HR ALL 2ND 1242.931 294059.9 4616488.5 175.99 177.3 0 16011808 KTDZ_KDTX_2016.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2015_CO.SUM CO 8-HR CLIFFS 2ND 1407.728 294183.7 4616339.7 178.97 189.12 0 15082616 KTDZ_KDTX_2015.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2014_CO.SUM CO 8-HR CLIFFS 2ND 1404.237 293760.4 4616655.2 179.58 179.58 0 14122608 KTDZ_KDTX_2014.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2017_CO.SUM CO 8-HR CLIFFS 2ND 1371.264 294156.1 4616380.5 177.5 188.85 0 17090716 KTDZ_KDTX_2017.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2013_CO.SUM CO 8-HR CLIFFS 2ND 1296.688 294114.8 4616441.6 176.57 185.8 0 13032108 KTDZ_KDTX_2013.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2016_CO.SUM CO 8-HR CLIFFS 2ND 1231.929 294211.3 4616298.9 179.85 189.12 0 16071516 KTDZ_KDTX_2016.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2014_CO.SUM CO 8-HR LT20K 2ND 1427.304 293760.4 4616655.2 179.58 179.58 0 14122608 KTDZ_KDTX_2014.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2015_CO.SUM CO 8-HR LT20K 2ND 1408.351 294183.7 4616339.7 178.97 189.12 0 15082616 KTDZ_KDTX_2015.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2017_CO.SUM CO 8-HR LT20K 2ND 1371.923 294156.1 4616380.5 177.5 188.85 0 17090716 KTDZ_KDTX_2017.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2013_CO.SUM CO 8-HR LT20K 2ND 1305.757 294114.8 4616441.6 176.57 185.8 0 13032108 KTDZ_KDTX_2013.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_2016_CO.SUM CO 8-HR LT20K 2ND 1232.186 294211.3 4616298.9 179.85 189.12 0 16071516 KTDZ_KDTX_2016.SFC 603 3 1221AERMOD 18081 IronUnits NAAQS_5yrs_NO2.SUM NO2 8TH-HIGHEST MAX DAILY 1-HR ALL 1ST 168.4834 293000 4617150 173.26 173.26 0 5 YEARS KTDZ_KDTX_2013_2017.SFC 261 3 726AERMOD 18081 IronUnits NAAQS_5yrs_NO2.SUM NO2 8TH-HIGHEST MAX DAILY 1-HR CLIFFS 1ST 8.96227 294200 4616350 182.19 188.98 0 5 YEARS KTDZ_KDTX_2013_2017.SFC 261 3 726AERMOD 18081 IronUnits NAAQS_5yrs_NO2.SUM NO2 8TH-HIGHEST MAX DAILY 1-HR LT20K 1ST 106.1313 293000 4617150 173.26 173.26 0 5 YEARS KTDZ_KDTX_2013_2017.SFC 261 3 726AERMOD 18081 IronUnits NAAQS_2015_NOX.SUM NOX ANNUAL ALL 1ST 7.51554 293928.5 4616620.2 179.25 179.25 0 1 YEARS KTDZ_KDTX_2015.SFC 265 3 29AERMOD 18081 IronUnits NAAQS_2016_NOX.SUM NOX ANNUAL ALL 1ST 7.47285 293969.2 4616591 179.14 179.14 0 1 YEARS KTDZ_KDTX_2016.SFC 265 3 29AERMOD 18081 IronUnits NAAQS_2014_NOX.SUM NOX ANNUAL ALL 1ST 7.43046 293883.8 4616620.7 179.33 179.33 0 1 YEARS KTDZ_KDTX_2014.SFC 265 3 29AERMOD 18081 IronUnits NAAQS_2017_NOX.SUM NOX ANNUAL ALL 1ST 7.1928 293928.5 4616620.2 179.25 179.25 0 1 YEARS KTDZ_KDTX_2017.SFC 265 3 29AERMOD 18081 IronUnits NAAQS_2013_NOX.SUM NOX ANNUAL ALL 1ST 6.9343 293986.5 4616579.2 179.19 179.19 0 1 YEARS KTDZ_KDTX_2013.SFC 265 3 29AERMOD 18081 IronUnits NAAQS_2014_NOX.SUM NOX ANNUAL CLIFFS 1ST 1.2532 293883.8 4616620.7 179.33 179.33 0 1 YEARS KTDZ_KDTX_2014.SFC 265 3 29AERMOD 18081 IronUnits NAAQS_2015_NOX.SUM NOX ANNUAL CLIFFS 1ST 1.24486 293906.1 4616620.5 179.22 179.22 0 1 YEARS KTDZ_KDTX_2015.SFC 265 3 29AERMOD 18081 IronUnits NAAQS_2017_NOX.SUM NOX ANNUAL CLIFFS 1ST 1.15961 293928.5 4616620.2 179.25 179.25 0 1 YEARS KTDZ_KDTX_2017.SFC 265 3 29AERMOD 18081 IronUnits NAAQS_2016_NOX.SUM NOX ANNUAL CLIFFS 1ST 1.13884 293969.2 4616591 179.14 179.14 0 1 YEARS KTDZ_KDTX_2016.SFC 265 3 29AERMOD 18081 IronUnits NAAQS_2013_NOX.SUM NOX ANNUAL CLIFFS 1ST 1.09651 293906.1 4616620.5 179.22 179.22 0 1 YEARS KTDZ_KDTX_2013.SFC 265 3 29AERMOD 18081 IronUnits NAAQS_2016_NOX.SUM NOX ANNUAL LT20K 1ST 6.41036 293969.2 4616591 179.14 179.14 0 1 YEARS KTDZ_KDTX_2016.SFC 265 3 29AERMOD 18081 IronUnits NAAQS_2014_NOX.SUM NOX ANNUAL LT20K 1ST 6.37956 293883.8 4616620.7 179.33 179.33 0 1 YEARS KTDZ_KDTX_2014.SFC 265 3 29AERMOD 18081 IronUnits NAAQS_2015_NOX.SUM NOX ANNUAL LT20K 1ST 6.29748 293928.5 4616620.2 179.25 179.25 0 1 YEARS KTDZ_KDTX_2015.SFC 265 3 29AERMOD 18081 IronUnits NAAQS_2017_NOX.SUM NOX ANNUAL LT20K 1ST 6.08532 293928.5 4616620.2 179.25 179.25 0 1 YEARS KTDZ_KDTX_2017.SFC 265 3 29AERMOD 18081 IronUnits NAAQS_2013_NOX.SUM NOX ANNUAL LT20K 1ST 5.93343 293986.5 4616579.2 179.19 179.19 0 1 YEARS KTDZ_KDTX_2013.SFC 265 3 29AERMOD 18081 IronUnits NAAQS_5yrs_PM10.SUM PM10 24-HR ALL 6TH 45.21494 292350 4616000 181.9 181.9 0 16081624 KTDZ_KDTX_2013_2017.SFC 458 3 1793AERMOD 18081 IronUnits NAAQS_5yrs_PM10.SUM PM10 24-HR CLIFFS 6TH 18.73093 293407.6 4616618.5 179.63 179.63 0 17122824 KTDZ_KDTX_2013_2017.SFC 458 3 1793AERMOD 18081 IronUnits NAAQS_5yrs_PM10.SUM PM10 24-HR LT20K 6TH 43.94912 292350 4616000 181.9 181.9 0 15083124 KTDZ_KDTX_2013_2017.SFC 458 3 1793AERMOD 18081 IronUnits NAAQS_5yrs_PM25.SUM PM25 8TH-HIGHEST 24-HR ALL 1ST 9.37874 290900 4616400 181.5 181.5 0 5 YEARS KTDZ_KDTX_2013_2017.SFC 409 3 3781AERMOD 18081 IronUnits NAAQS_5yrs_PM25.SUM PM25 8TH-HIGHEST 24-HR CLIFFS 1ST 5.47714 293582.9 4616123.2 180.59 180.59 0 5 YEARS KTDZ_KDTX_2013_2017.SFC 409 3 3781AERMOD 18081 IronUnits NAAQS_5yrs_PM25.SUM PM25 8TH-HIGHEST 24-HR LT20K 1ST 8.04536 290900 4616400 181.5 181.5 0 5 YEARS KTDZ_KDTX_2013_2017.SFC 409 3 3781AERMOD 18081 IronUnits NAAQS_5yrs_PM-25.SUM PM-25 ANNUAL ALL 1ST 2.6073 294003.8 4616567.3 178.9 178.9 0 5 YEARS KTDZ_KDTX_2013_2017.SFC 417 3 1251AERMOD 18081 IronUnits NAAQS_5yrs_PM-25.SUM PM-25 ANNUAL CLIFFS 1ST 0.9649 294003.8 4616567.3 178.9 178.9 0 5 YEARS KTDZ_KDTX_2013_2017.SFC 417 3 1251AERMOD 18081 IronUnits NAAQS_5yrs_PM-25.SUM PM-25 ANNUAL LT20K 1ST 2.03192 294003.8 4616567.3 178.9 178.9 0 5 YEARS KTDZ_KDTX_2013_2017.SFC 417 3 1251

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Iron Units HBI NAAQS Analysis (9-13-19)

Pollutant Average Group Rank

Model Conc.

(ug/m3)Background

(ug/m3)

Secondary PM2.5

(ug/m3)Total

(ug/m3)Standard (ug/m3) % Standard Comments

NO2 8TH-HIGHEST MAX DAILY 1-HR ALL 1ST 168.48 Note 9 NA 168.5 188.0 90%NOX ANNUAL ALL 1ST 7.52 17.68 NA 25.2 100.0 25%

PM25 8TH-HIGHEST 24-HR ALL 1ST 9.38 21.5 0.07 30.9 35.0 88%PM-25 ANNUAL LT20K 1ST 2.03 8.22 0.002 10.3 12.0 85% Only offsite sources within 20km included.

CO 1-HR ALL 2ND 2844.89 2,743 NA 5588.1 40,000 14%CO 8-HR ALL 2ND 1429.30 1,863 NA 3292.4 10,000 33%

PM10 24-HR ALL 6TH 45.21 35.0 NA 80.2 150.0 53%Notes:

1) 1-hr NOx to NO2 conversion for assessing NAAQS assumes PVMRM with a Cliffs instack NO2/NOx ratio of 0.5. 0.2 used for offsite sources. Hourly O3 data from Toledo (AQS 39-095-0024).2) Short-term standards exclude emergency generator and flare.3) Secondary PM2.5 formation calculated using MERPs approach. See attached MERPS calculation.4) Potential emissions modeled for all sources.5) Background PM2.5 values from State Road Park in Monroe, MI (AQS 16-115-0006, 2015-17). PM10 and NO2 from and Cleveland (AQS 39-093-3002 and 39-035-0073, respectively, also 2015-17). 6) Background CO values from Allen Park (AQS 26-163-0001, 2015-17)7) Only includes receptors where Iron Units impacts significant.8) NA - not applicable9) Season by hour background values added within model.

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Iron Units HBI Increment Analysis (9-9-19)Model File Pollutant Average Group Rank Conc/Dep East (X) North (Y) Elev Hill Flag Time Met File Sources Groups ReceptorsAERMOD 18081 IronUnits Increment_2015_NOX.SUM NOX ANNUAL ALL 1ST 7.51554 293928.5 4616620.2 179.25 179.25 0 1 YEARS KTDZ_KDTX_2015.SFC 265 4 29AERMOD 18081 IronUnits Increment_2016_NOX.SUM NOX ANNUAL ALL 1ST 7.47285 293969.2 4616591 179.14 179.14 0 1 YEARS KTDZ_KDTX_2016.SFC 265 4 29AERMOD 18081 IronUnits Increment_2014_NOX.SUM NOX ANNUAL ALL 1ST 7.43046 293883.8 4616620.7 179.33 179.33 0 1 YEARS KTDZ_KDTX_2014.SFC 265 4 29AERMOD 18081 IronUnits Increment_2017_NOX.SUM NOX ANNUAL ALL 1ST 7.1928 293928.5 4616620.2 179.25 179.25 0 1 YEARS KTDZ_KDTX_2017.SFC 265 4 29AERMOD 18081 IronUnits Increment_2013_NOX.SUM NOX ANNUAL ALL 1ST 6.9343 293986.5 4616579.2 179.19 179.19 0 1 YEARS KTDZ_KDTX_2013.SFC 265 4 29AERMOD 18081 IronUnits Increment_2014_NOX.SUM NOX ANNUAL CLIFFS 1ST 1.2532 293883.8 4616620.7 179.33 179.33 0 1 YEARS KTDZ_KDTX_2014.SFC 265 4 29AERMOD 18081 IronUnits Increment_2015_NOX.SUM NOX ANNUAL CLIFFS 1ST 1.24486 293906.1 4616620.5 179.22 179.22 0 1 YEARS KTDZ_KDTX_2015.SFC 265 4 29AERMOD 18081 IronUnits Increment_2017_NOX.SUM NOX ANNUAL CLIFFS 1ST 1.15961 293928.5 4616620.2 179.25 179.25 0 1 YEARS KTDZ_KDTX_2017.SFC 265 4 29AERMOD 18081 IronUnits Increment_2016_NOX.SUM NOX ANNUAL CLIFFS 1ST 1.13884 293969.2 4616591 179.14 179.14 0 1 YEARS KTDZ_KDTX_2016.SFC 265 4 29AERMOD 18081 IronUnits Increment_2013_NOX.SUM NOX ANNUAL CLIFFS 1ST 1.09651 293906.1 4616620.5 179.22 179.22 0 1 YEARS KTDZ_KDTX_2013.SFC 265 4 29AERMOD 18081 IronUnits Increment_2016_NOX.SUM NOX ANNUAL PM10INC 1ST 5.14462 293969.2 4616591 179.14 179.14 0 1 YEARS KTDZ_KDTX_2016.SFC 265 4 29AERMOD 18081 IronUnits Increment_2014_NOX.SUM NOX ANNUAL PM10INC 1ST 5.13795 293883.8 4616620.7 179.33 179.33 0 1 YEARS KTDZ_KDTX_2014.SFC 265 4 29AERMOD 18081 IronUnits Increment_2015_NOX.SUM NOX ANNUAL PM10INC 1ST 4.91048 293928.5 4616620.2 179.25 179.25 0 1 YEARS KTDZ_KDTX_2015.SFC 265 4 29AERMOD 18081 IronUnits Increment_2017_NOX.SUM NOX ANNUAL PM10INC 1ST 4.83479 293928.5 4616620.2 179.25 179.25 0 1 YEARS KTDZ_KDTX_2017.SFC 265 4 29AERMOD 18081 IronUnits Increment_2013_NOX.SUM NOX ANNUAL PM10INC 1ST 4.80454 293986.5 4616579.2 179.19 179.19 0 1 YEARS KTDZ_KDTX_2013.SFC 265 4 29AERMOD 18081 IronUnits Increment_2014_NOX.SUM NOX ANNUAL PM25INC 1ST 1.51377 293883.8 4616620.7 179.33 179.33 0 1 YEARS KTDZ_KDTX_2014.SFC 265 4 29AERMOD 18081 IronUnits Increment_2015_NOX.SUM NOX ANNUAL PM25INC 1ST 1.5046 293906.1 4616620.5 179.22 179.22 0 1 YEARS KTDZ_KDTX_2015.SFC 265 4 29AERMOD 18081 IronUnits Increment_2016_NOX.SUM NOX ANNUAL PM25INC 1ST 1.45242 293969.2 4616591 179.14 179.14 0 1 YEARS KTDZ_KDTX_2016.SFC 265 4 29AERMOD 18081 IronUnits Increment_2017_NOX.SUM NOX ANNUAL PM25INC 1ST 1.43179 293928.5 4616620.2 179.25 179.25 0 1 YEARS KTDZ_KDTX_2017.SFC 265 4 29AERMOD 18081 IronUnits Increment_2013_NOX.SUM NOX ANNUAL PM25INC 1ST 1.3603 293906.1 4616620.5 179.22 179.22 0 1 YEARS KTDZ_KDTX_2013.SFC 265 4 29AERMOD 18081 IronUnits Increment_2015_PM10.SUM PM10 24-HR ALL 2ND 54.58736 292400 4615950 182.33 182.33 0 15090324 KTDZ_KDTX_2015.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2013_PM10.SUM PM10 24-HR ALL 2ND 45.28208 292450 4615950 182.32 182.32 0 13071724 KTDZ_KDTX_2013.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2016_PM10.SUM PM10 24-HR ALL 2ND 45.21494 292350 4616000 181.9 181.9 0 16081624 KTDZ_KDTX_2016.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2017_PM10.SUM PM10 24-HR ALL 2ND 45.0588 294003.8 4616567.3 178.9 178.9 0 17122724 KTDZ_KDTX_2017.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2014_PM10.SUM PM10 24-HR ALL 2ND 33.89516 293430.3 4616650.7 179.52 179.52 0 14122024 KTDZ_KDTX_2014.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2014_PM10.SUM PM10 24-HR CLIFFS 2ND 23.49066 293451.3 4616665.7 179.76 179.76 0 14122124 KTDZ_KDTX_2014.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2017_PM10.SUM PM10 24-HR CLIFFS 2ND 20.9952 294003.8 4616567.3 178.9 178.9 0 17011524 KTDZ_KDTX_2017.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2016_PM10.SUM PM10 24-HR CLIFFS 2ND 20.01831 293407.6 4616618.5 179.63 179.63 0 16101424 KTDZ_KDTX_2016.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2015_PM10.SUM PM10 24-HR CLIFFS 2ND 19.41098 294003.8 4616567.3 178.9 178.9 0 15090224 KTDZ_KDTX_2015.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2013_PM10.SUM PM10 24-HR CLIFFS 2ND 15.98571 293393.9 4616597.9 179.5 179.5 0 13012524 KTDZ_KDTX_2013.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2014_PM10.SUM PM10 24-HR PM10INC 2ND 26.29669 293430.3 4616650.7 179.52 179.52 0 14122024 KTDZ_KDTX_2014.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2016_PM10.SUM PM10 24-HR PM10INC 2ND 24.17446 293407.6 4616618.5 179.63 179.63 0 16101424 KTDZ_KDTX_2016.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2017_PM10.SUM PM10 24-HR PM10INC 2ND 23.89219 293352.8 4616536.2 178.96 185.08 0 17122824 KTDZ_KDTX_2017.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2015_PM10.SUM PM10 24-HR PM10INC 2ND 23.48208 293692.2 4616718.8 179.8 179.8 0 15022824 KTDZ_KDTX_2015.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2013_PM10.SUM PM10 24-HR PM10INC 2ND 17.6643 293582.9 4616123.2 180.59 180.59 0 13120224 KTDZ_KDTX_2013.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2014_PM10.SUM PM10 24-HR PM25INC 2ND 23.64373 293451.3 4616665.7 179.76 179.76 0 14122124 KTDZ_KDTX_2014.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2017_PM10.SUM PM10 24-HR PM25INC 2ND 21.48012 294003.8 4616567.3 178.9 178.9 0 17011524 KTDZ_KDTX_2017.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2016_PM10.SUM PM10 24-HR PM25INC 2ND 20.09293 293407.6 4616618.5 179.63 179.63 0 16101424 KTDZ_KDTX_2016.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2015_PM10.SUM PM10 24-HR PM25INC 2ND 19.52302 294003.8 4616567.3 178.9 178.9 0 15090224 KTDZ_KDTX_2015.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2013_PM10.SUM PM10 24-HR PM25INC 2ND 16.02566 293393.9 4616597.9 179.5 179.5 0 13012524 KTDZ_KDTX_2013.SFC 458 4 1793AERMOD 18081 IronUnits Increment_2015_PM-10.SUM PM-10 ANNUAL ALL 1ST 7.65803 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2015.SFC 466 4 178AERMOD 18081 IronUnits Increment_2016_PM-10.SUM PM-10 ANNUAL ALL 1ST 7.05706 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2016.SFC 466 4 178AERMOD 18081 IronUnits Increment_2014_PM-10.SUM PM-10 ANNUAL ALL 1ST 6.98405 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2014.SFC 466 4 178AERMOD 18081 IronUnits Increment_2017_PM-10.SUM PM-10 ANNUAL ALL 1ST 6.96578 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2017.SFC 466 4 178AERMOD 18081 IronUnits Increment_2013_PM-10.SUM PM-10 ANNUAL ALL 1ST 6.0451 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2013.SFC 466 4 178AERMOD 18081 IronUnits Increment_2015_PM-10.SUM PM-10 ANNUAL CLIFFS 1ST 2.50622 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2015.SFC 466 4 178AERMOD 18081 IronUnits Increment_2014_PM-10.SUM PM-10 ANNUAL CLIFFS 1ST 2.22577 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2014.SFC 466 4 178AERMOD 18081 IronUnits Increment_2016_PM-10.SUM PM-10 ANNUAL CLIFFS 1ST 2.20537 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2016.SFC 466 4 178AERMOD 18081 IronUnits Increment_2017_PM-10.SUM PM-10 ANNUAL CLIFFS 1ST 2.20508 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2017.SFC 466 4 178AERMOD 18081 IronUnits Increment_2013_PM-10.SUM PM-10 ANNUAL CLIFFS 1ST 2.05358 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2013.SFC 466 4 178AERMOD 18081 IronUnits Increment_2015_PM-10.SUM PM-10 ANNUAL PM10INC 1ST 4.20047 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2015.SFC 466 4 178AERMOD 18081 IronUnits Increment_2014_PM-10.SUM PM-10 ANNUAL PM10INC 1ST 4.02266 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2014.SFC 466 4 178AERMOD 18081 IronUnits Increment_2016_PM-10.SUM PM-10 ANNUAL PM10INC 1ST 3.94223 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2016.SFC 466 4 178AERMOD 18081 IronUnits Increment_2017_PM-10.SUM PM-10 ANNUAL PM10INC 1ST 3.77848 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2017.SFC 466 4 178AERMOD 18081 IronUnits Increment_2013_PM-10.SUM PM-10 ANNUAL PM10INC 1ST 3.48373 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2013.SFC 466 4 178AERMOD 18081 IronUnits Increment_2015_PM-10.SUM PM-10 ANNUAL PM25INC 1ST 2.63981 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2015.SFC 466 4 178AERMOD 18081 IronUnits Increment_2014_PM-10.SUM PM-10 ANNUAL PM25INC 1ST 2.35451 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2014.SFC 466 4 178AERMOD 18081 IronUnits Increment_2017_PM-10.SUM PM-10 ANNUAL PM25INC 1ST 2.34893 293200 4617050 176.94 176.94 0 1 YEARS KTDZ_KDTX_2017.SFC 466 4 178AERMOD 18081 IronUnits Increment_2016_PM-10.SUM PM-10 ANNUAL PM25INC 1ST 2.34653 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2016.SFC 466 4 178AERMOD 18081 IronUnits Increment_2013_PM-10.SUM PM-10 ANNUAL PM25INC 1ST 2.17348 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2013.SFC 466 4 178AERMOD 18081 IronUnits Increment_2017_PM25.SUM PM25 24-HR ALL 2ND 38.84726 290900 4616400 181.5 181.5 0 17011424 KTDZ_KDTX_2017.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2016_PM25.SUM PM25 24-HR ALL 2ND 38.80585 290900 4616400 181.5 181.5 0 16050324 KTDZ_KDTX_2016.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2014_PM25.SUM PM25 24-HR ALL 2ND 35.93762 290900 4616400 181.5 181.5 0 14122824 KTDZ_KDTX_2014.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2015_PM25.SUM PM25 24-HR ALL 2ND 29.80462 290900 4616400 181.5 181.5 0 15012224 KTDZ_KDTX_2015.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2013_PM25.SUM PM25 24-HR ALL 2ND 29.5512 290900 4616400 181.5 181.5 0 13030424 KTDZ_KDTX_2013.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2017_PM25.SUM PM25 24-HR CLIFFS 2ND 7.02155 293582.9 4616123.2 180.59 180.59 0 17122224 KTDZ_KDTX_2017.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2016_PM25.SUM PM25 24-HR CLIFFS 2ND 6.79367 294003.8 4616567.3 178.9 178.9 0 16110524 KTDZ_KDTX_2016.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2015_PM25.SUM PM25 24-HR CLIFFS 2ND 6.63769 293582.9 4616123.2 180.59 180.59 0 15050624 KTDZ_KDTX_2015.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2013_PM25.SUM PM25 24-HR CLIFFS 2ND 6.16414 293582.9 4616123.2 180.59 180.59 0 13092324 KTDZ_KDTX_2013.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2014_PM25.SUM PM25 24-HR CLIFFS 2ND 6.09279 293582.9 4616123.2 180.59 180.59 0 14092724 KTDZ_KDTX_2014.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2017_PM25.SUM PM25 24-HR PM10INC 2ND 38.54422 290900 4616400 181.5 181.5 0 17011424 KTDZ_KDTX_2017.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2016_PM25.SUM PM25 24-HR PM10INC 2ND 37.95402 290900 4616400 181.5 181.5 0 16050324 KTDZ_KDTX_2016.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2014_PM25.SUM PM25 24-HR PM10INC 2ND 35.88547 290900 4616400 181.5 181.5 0 14122824 KTDZ_KDTX_2014.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2013_PM25.SUM PM25 24-HR PM10INC 2ND 29.21276 290900 4616400 181.5 181.5 0 13030424 KTDZ_KDTX_2013.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2015_PM25.SUM PM25 24-HR PM10INC 2ND 28.86293 290900 4616400 181.5 181.5 0 15071024 KTDZ_KDTX_2015.SFC 409 4 3781

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AERMOD 18081 IronUnits Increment_2017_PM25.SUM PM25 24-HR PM25INC 2ND 7.16375 293582.9 4616123.2 180.59 180.59 0 17010224 KTDZ_KDTX_2017.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2016_PM25.SUM PM25 24-HR PM25INC 2ND 6.79945 294003.8 4616567.3 178.9 178.9 0 16110524 KTDZ_KDTX_2016.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2015_PM25.SUM PM25 24-HR PM25INC 2ND 6.66021 293582.9 4616123.2 180.59 180.59 0 15050624 KTDZ_KDTX_2015.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2014_PM25.SUM PM25 24-HR PM25INC 2ND 6.24803 293582.9 4616123.2 180.59 180.59 0 14010124 KTDZ_KDTX_2014.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2013_PM25.SUM PM25 24-HR PM25INC 2ND 6.18637 293582.9 4616123.2 180.59 180.59 0 13092324 KTDZ_KDTX_2013.SFC 409 4 3781AERMOD 18081 IronUnits Increment_2015_PM-25.SUM PM-25 ANNUAL ALL 1ST 2.87879 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2015.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2017_PM-25.SUM PM-25 ANNUAL ALL 1ST 2.63519 293582.9 4616123.2 180.59 180.59 0 1 YEARS KTDZ_KDTX_2017.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2016_PM-25.SUM PM-25 ANNUAL ALL 1ST 2.58225 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2016.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2014_PM-25.SUM PM-25 ANNUAL ALL 1ST 2.57877 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2014.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2013_PM-25.SUM PM-25 ANNUAL ALL 1ST 2.39123 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2013.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2015_PM-25.SUM PM-25 ANNUAL CLIFFS 1ST 1.06524 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2015.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2014_PM-25.SUM PM-25 ANNUAL CLIFFS 1ST 0.95362 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2014.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2017_PM-25.SUM PM-25 ANNUAL CLIFFS 1ST 0.95133 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2017.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2016_PM-25.SUM PM-25 ANNUAL CLIFFS 1ST 0.94106 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2016.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2013_PM-25.SUM PM-25 ANNUAL CLIFFS 1ST 0.91323 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2013.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2015_PM-25.SUM PM-25 ANNUAL PM10INC 1ST 1.85559 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2015.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2014_PM-25.SUM PM-25 ANNUAL PM10INC 1ST 1.75777 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2014.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2016_PM-25.SUM PM-25 ANNUAL PM10INC 1ST 1.74548 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2016.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2017_PM-25.SUM PM-25 ANNUAL PM10INC 1ST 1.68782 293582.9 4616123.2 180.59 180.59 0 1 YEARS KTDZ_KDTX_2017.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2013_PM-25.SUM PM-25 ANNUAL PM10INC 1ST 1.60749 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2013.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2015_PM-25.SUM PM-25 ANNUAL PM25INC 1ST 1.18075 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2015.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2017_PM-25.SUM PM-25 ANNUAL PM25INC 1ST 1.07353 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2017.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2014_PM-25.SUM PM-25 ANNUAL PM25INC 1ST 1.06273 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2014.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2016_PM-25.SUM PM-25 ANNUAL PM25INC 1ST 1.06129 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2016.SFC 417 4 1251AERMOD 18081 IronUnits Increment_2013_PM-25.SUM PM-25 ANNUAL PM25INC 1ST 1.01401 294003.8 4616567.3 178.9 178.9 0 1 YEARS KTDZ_KDTX_2013.SFC 417 4 1251

Iron Units HBI Increment Analysis (9-9-19)

Pollutant Average Group Rank

Model Conc.

(ug/m3)

Secondary PM2.5

(ug/m3)Total

(ug/m3)Standard (ug/m3) % Standard Analysis Comments

PM25 24-HR PM25INC 2ND 7.16 0.070 7.23 9.0 80% 100% Increment Cumulative impacts, Cliffs and other increment consumers.PM25 24-HR CLIFFS 2ND 7.02 0.070 7.09 4.5 158% 50% Increment Cliffs impacts only. PM25 24-HR CLIFFS 2ND 7.02 0.070 7.09 7.5 95% 83% Increment Cliffs impacts only. PM-25 ANNUAL PM25INC 1ST 1.18 0.002 1.18 4.0 30% 100% Increment Cumulative impacts, Cliffs and other increment consumers.PM-25 ANNUAL CLIFFS 1ST 1.07 0.002 1.07 2.0 53% 50% Increment Cliffs impacts only.

PM10 24-HR PM10INC 2ND 26.30 NA 26.30 30.0 88% 100% Increment Cumulative impacts, Cliffs and other inc consumers. Note 5.PM10 24-HR CLIFFS 2ND 23.49 NA 23.49 15.0 157% 50% Increment Cliffs impacts only. PM10 24-HR CLIFFS 2ND 23.49 NA 23.49 24.9 94% 83% Increment Cliffs impacts only. PM-10 ANNUAL PM10INC 1ST 4.20 NA 4.20 17.0 25% 100% Increment Cumulative impacts, Cliffs and other increment consumers.PM-10 ANNUAL CLIFFS 1ST 2.51 NA 2.51 8.5 29% 50% Increment Cliffs impacts only.

NOX ANNUAL ALL 1ST 7.52 NA 7.52 25.0 30% 100% Increment Cumulative impacts, Cliffs and other increment consumers.NOX ANNUAL CLIFFS 1ST 1.25 NA 1.25 12.5 10% 50% Increment Cliffs impacts only. 1) Off-site sources within 50km evaluated for inclusion.2) Secondary PM2.5 formation calculated using MERPs approach. See attached MERPS calculation.3) Potential emissions conservatively modeled for offsite sources.4) Only includes receptors where Iron Units impacts significant.5) Cliffs not significant as paired in time and space. Max = 0.047 ug/m3.

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PM2.5 MERP Calculation (Use Source 11, Macomb, MI - 500 TPY, 90m Release)

Precursor

Modeled Emissions of Hypothetical

Source (MER) (TPY)

Release Height of Hypothetical

Source

Max 24-hr Impact of

Hypothetical Source (MIHS)

(ug/m3)

Calculated 24-hr Class II MERP

(TPY)

Max Annual Impact of

Hypothetical Source (MIHS)

(ug/m3)

Calculated Annual Class II

MERP (TPY)

24-hr Contribution

(ug/m3)

Annual Contribution

(ug/m3)NOx 500 H 0.060 10000.0 0.002 47889.5 0.057 0.002SO2 500 H 0.242 2479.3 0.004 25493.6 0.012 0.0002

Total 0.070 0.002MERP Calculation = Critical Air Quality Threshold (CAC, PM2.5 SILs) X [Modeled Emission Rate from Source 11 (MER)

/Modeled Impact from Source 10 (MIHS)]

Contribution = max impact hypothetical source divided by emissions of hypo source multiplied by the project emissionsExample 24hr NOx:0.06 ug/m3 divided by 500 TPY times 479 TPY = 0.06 ug/m3

Secondary PM2.5 Impact Calculation - Cummulative NAAQSSecondary NOx Contribution Secondary SO2 Contribution

Average

Background PM2.5

Concentration (ug/m3)

Model (MDC) (ug/m3)

Emissions (NOxP) (TPY) MERP (TPY)

Emissions (SO2P) (TPY) MERP (TPY)

Critical Air Quality

Threshold (CAC)

(ug/m3)Total (AQI)

(ug/m3) NAAQS % NAAQS24-hr 21.5 94.52 478.7 10000.0 25.2 2479.3 1.20 116.09 35 331.7%Annual 8.22 3.14 478.7 47889.5 25.2 25493.6 0.20 11.37 12 94.7%Where:NAAQS Calculation: Total Air Quality Impact (AQI) = Background PM2.5 + Modeled Direct PM2.5 Concentration + (NOxP/NOx MERP) + (SO2P/SO2 MERP) * CACCAC = PM2.5 Class II SILs

Secondary PM2.5 Impact Calculation - Cummulative IncrementSecondary NOx Contribution Secondary SO2 Contribution

Average

Background PM2.5

Concentration (ug/m3)

Model (MDC) (ug/m3)

Emissions (NOxP) (TPY) MERP (TPY)

Emissions (SO2P) (TPY) MERP (TPY)

Critical Air Quality

Threshold (CAC)

(ug/m3)Total (AQI)

(ug/m3) Increment%

Increment24-hr NA 0.93 478.7 10000.0 25.2 2479.3 1.20 1.00 9 11.1%Annual NA 0.00 478.7 47889.5 25.2 25493.6 0.20 0.00 4 0.1%Where:Increment Calculation: Total Air Quality Impact (AQI) = Modeled Direct PM2.5 Concentration + (NOxP/NOx MERP) + (SO2P/SO2 MERP) * CACCAC = PM2.5 Class II SILsNA - Not Applicable. Background concentration not considered in increment analysis.

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Ozone MERP Calculation (Use Source 11, Macomb, MI - 500 TPY, 90m Release)

Precursor

Modeled Emissions of Hypothetical

Source (MER) (TPY)

Release Height of Hypothetical

Source

Max 8-hr Impact of Hypothetical Source (MIHS)

(ppb)Calculated 8-hr

MERP (TPY)NOx 500 H 0.936 534.2VOC 500 H 0.281 1779.4MERP = Critical Air Quality Threshold (CAC, O3 SIL of 1.0 ppb) X [Modeled Emission Rate from Source 10 (MER)/Modeled Impact from Source 11 (MIHS)]

Ozone Impact CalculationNOx Contribution VOC Contribution

Average

Project Emissions

(NOxP) (TPY) MERP (TPY) % Contribution

Project Emissions

(VOCP) (TPY) MERP (TPY)%

Contribution Total (AQI)8-hr 478.7 534.2 89.61% 16.40 1779.4 0.92% 90.53%Where:Total Air Quality Impact (AQI) = [Project NOx Emissions (NOxP)/NOx MERP] + [Project VOC Emissions (VOCP)/VOC MERP]

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F:\My Docs\RTPENV\Projects\Cliffs\Toledo\2019 Model Update\VISCREEN\HBI.sumPrinted on Tuesday, July 30, 2019 at 13:51:26 Page 1 of 1

0102 Visual Effects Screening Analysis for03 Source: Iron Units HBI 04 Class I Area: Cuyahoga NP 050607 *** Level-1 Screening ***08 Input Emissions for 0910 Particulates 33.00 LB /HR 11 NOx (as NO2) 109.00 LB /HR 12 Primary NO2 0.00 LB /HR 13 Soot 0.00 LB /HR 14 Primary SO4 0.00 LB /HR 15 1617 **** Default Particle Characteristics Assumed1819 Transport Scenario Specifications:2021 Background Ozone: 0.04 ppm22 Background Visual Range: 25.00 km23 Source-Observer Distance: 155.00 km24 Min. Source-Class I Distance: 155.00 km25 Max. Source-Class I Distance: 175.00 km26 Plume-Source-Observer Angle: 11.25 degrees27 Stability: 628 Wind Speed: 1.00 m/s2930 R E S U L T S3132 Asterisks (*) indicate plume impacts that exceed screening criteria3334 Maximum Visual Impacts INSIDE Class I Area35 Screening Criteria ARE NOT Exceeded36 Delta E Contrast37 =========== ============38 Backgrnd Theta Azi Distance Alpha Crit Plume Crit Plume39 ======== ===== === ======== ===== ==== ===== ==== =====40 SKY 10. 84. 155.0 84. 2.00 0.003 0.05 0.000 41 SKY 140. 84. 155.0 84. 2.00 0.001 0.05 0.000 42 TERRAIN 10. 84. 155.0 84. 2.00 0.000 0.05 0.000 43 TERRAIN 140. 84. 155.0 84. 2.00 0.000 0.05 0.000 44 4546 Maximum Visual Impacts OUTSIDE Class I Area47 Screening Criteria ARE NOT Exceeded48 Delta E Contrast49 =========== ============50 Backgrnd Theta Azi Distance Alpha Crit Plume Crit Plume51 ======== ===== === ======== ===== ==== ===== ==== =====52 SKY 10. 75. 150.0 94. 2.00 0.004 0.05 0.000 53 SKY 140. 75. 150.0 94. 2.00 0.001 0.05 0.000 54 TERRAIN 10. 55. 138.7 114. 2.00 0.000 0.05 0.000 55 TERRAIN 140. 55. 138.7 114. 2.00 0.000 0.05 0.000

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Appendix E – Exempt Natural Gas Combustion Equipment

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Exempt Natural Gas Combustion Equipment Proposed as Part of the HBI Project

Heat Input (MMBtu/hour) Number of units 0.15 4 0.20 22 0.25 7 0.40 1 0.45 1 0.75 5 ≤0.10 40

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Appendix F – Process Flow Diagram

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NOTE: Material handling for boat offloading and material transfer up to and inclusive of CV-F03 hopper feed is out of the scope of this permit (e.g. completed by separate owner/operator)
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