Data sheet for cooling Tower

Bid Boland Gas Treating Plant II (Package A)

IRANIAN ENGINEERING & DEVELOPMENT GAS CO.

Consortium’s Job No.:7942

COOLING TOWER PACKAGES DUTY SPECIFICATIONS

Client’s Job No.:38687901

FEED Document No N/A Page 1 of 22

Owner Document Number: DS-444-47-002 Rev: 1a

Contractor Document Number: 7942-U444-FEQ-DAS-7002 D2

1a 29-Apr-09 D2 Issue for design V.S O.M/Sh.B F.T

0 02-9-12 D2 Issue for design PM MR PM

Rev. Date Status Description Prepared Checked Approved

DUTY SPECIFICATION FOR

COOLING TOWER PACKAGE ME-444-001 (INCLUDING ME-444-002 AND ME-444-003)

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PAGE No. REV. 1

PAGE No. REV. 1

01 02 03 04 05 06 07 08 09 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32









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TABLE OF CONTENTS

TABLE OF CONTENTS...........................................................................................................3

1 ABBREVIATIONS AND DEFINITIONS ..........................................................................5

1.1 Abbreviations ................................................................................................................5 1.2 Definitions......................................................................................................................7

2 INTRODUCTION.............................................................................................................8

2.1 Project Water Treatment Scope ...................................................................................8 2.2 Scope of Vendor for Cooling Tower and Associated Packages ...............................8 2.2.1 Cooling Tower (CT-444-001).......................................................................................8 2.2.2 Cooling Tower Chemical Package (ME-444-002) .....................................................9 2.2.3 Cooling Tower Filter Package (ME-444-003).............................................................9

3 CODES AND STANDARDS ...........................................................................................9

3.1 Job Specifications.......................................................................................................10 3.2 IPS Specification .........................................................................................................10

4 SUPPLY DESCRIPTION...............................................................................................12

4.1 Process Description....................................................................................................12 4.2 Feed Water Condition and Composition ...................................................................12 4.3 Product Water Specification.......................................................................................13 4.4 Chemical Specification ...............................................................................................13 4.5 Design Considerations ...............................................................................................13

5 GENERAL.....................................................................................................................14

5.1 Location .......................................................................................................................14 5.2 Utilities .........................................................................................................................14 5.2.1 Cooling Medium ........................................................................................................14 5.2.2 Heating Medium ........................................................................................................14 5.2.3 Cold Condensate.......................................................................................................14 5.2.4 Nitrogen System........................................................................................................14 5.2.5 Instrument Air / Plant Air..........................................................................................15 5.2.6 Electric Power ...........................................................................................................15 5.3 Site Data .......................................................................................................................15 5.3.1 Plot Plan.....................................................................................................................15 5.3.2 Design life ..................................................................................................................15 5.3.3 Environmental condition ..........................................................................................15

6 BASIC ENGINEERING REQUIREMENTS ...................................................................16









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6.1 General .........................................................................................................................16 6.2 Equipment Design Requirements ..............................................................................17 6.3 Turndown Ratio ...........................................................................................................17 6.4 Design Margin..............................................................................................................17 6.5 Heat Exchanger Design ..............................................................................................17 6.6 Vessel Design ..............................................................................................................17 6.7 Piping Design and Layout ..........................................................................................17 6.8 Metallurgy ....................................................................................................................17 6.9 Chemical and Catalysts ..............................................................................................18 6.10 Effluents.....................................................................................................................18 6.11 Operation ...................................................................................................................18 6.11.1 Operational Requirements .......................................................................................18

7 OTHER REQUIREMENTS............................................................................................19

8 REFERENCE DOCUMENTS ........................................................................................19

9 UNITS OF MEASUREMENTS ......................................................................................20

10 ATTACHMENTS ...........................................................................................................22









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1 ABBREVIATIONS AND DEFINITIONS

1.1 Abbreviations

AGRU: Acid Gas Removal Unit

AGDHU: Acid Gas De-hydration Unit

ANSI: American National Standard Institute

API: American Petroleum Institute

ASTM: American Society for Testing and Materials

BFW: Boiler Feed Water

BS: British Standard

OPEX / CAPEX: Operational Expenditure / CAPital EXpenditure

CW: Cooling Water

CP: Cathodic Protection for pipelines

CTR: Cost Time Resources

DC: Direct Current

DCS: Distributed Control System

DM Water: De-mineralised Water

EIA: Environmental Impact Assessment

EPIC: Engineering, Procurement, Installation and Commissioning

ESD: Emergency Shut-Down

FF: FOUNDATION™ Fieldbus

F&G: Fire & Gas

FRA: Fire Risk Assessment

GDS: Gas Distribution System

HART: Highway Addressable Remote Transducer

HAZID: Hazard Identification Study









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HAZOP: Hazard & Operability Study

HMI: Human Machine Interface

HP/MP/LP: High Pressure / Medium Pressure / Low Pressure

HVAC: Heating, Ventilation and Air Conditioning

IEA: Initial Environmental Approval

LER: Local Equipment Room

LLI: Long Lead Items (equipment)

LP: Low Pressure

MDEA: MethylDiEthanolAmine

MMSCFD: Million Standard Cubic Foot per Day

NACE: National Association of Corrosion Engineers

ONSAG: Stripped Associated Gas from onshore

PTF: Project Task Force

QRA: Quantitative Risk Assessment

RAG: Raw Associated Gas

RTU: Remote Telemetry Unit

SAFOP: Safety and Operability Study (Electrical Systems)

SCADA: Supervisory Control and Data Acquisition

SCENR: Supreme Council for the Environment & Natural Reserves

SG: Sour Gas from condensate fractionation unit

SOR: Statement of Requirement

SOW: Scope of Work

TEG: Tri Ethylene Glycol

IPS: Iranian Petroleum Standards









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1.2 Definitions

COMPANY: NIGC, owner and operator of the plant to be built, and decider of the project.

FEED: The phase of the Project that will define all project documentation necessary to handle the Engineering Procurement Installation & Commissioning (EPIC) phase.

EPC CONTRACTOR Means the Consortium of Sazeh – Jahanpars, in charge of the EPC of Bid Boland Gas Treating Plant Phase II engineering, procurement and construction.

FEED CONTRACTOR: Means SNC Lavalin, the company, employed by EPC Contractor, in charge of FEED Engineering design development.

VENDOR: Means a vendor which design, supply, and test the unit.









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2 INTRODUCTION NIGC is planning for construction of a new project, namely “Bid Boland Gas Treating Plant-II (BB2)'' located in the South West part of Iran, about 15 km North West of Behbahan city in Khuzestan province. Bid Boland Gas Treating Plant-II is comprised of industrial and non-industrial areas. The EPC for the Project has been split to two packages. Package A that consists of the main gas treating plant located in near Behbahan City, and the Package B that comprise of the storage and loading facilities located in Mahshahr by the Persian Gulf Coast plus the feed and product pipelines between the gas plant and the storage facilities. Raw water is supplied from Marun River to the Gas Treating Plant via pipeline and treated for the process and utility use.

2.1 Project Water Treatment Scope

The water treatment areas of the project consist of the following units:

1. Water Storage Tanks

2. Water Softening Unit (Cold Lime Softening)

3. Chemical Preparation and Injection Units

4. Media Filtration Units

5. RO Membrane Unit

6. Mixed Bed Ion Exchange Unit

7. Potable Water Unit

8. Cooling Tower

9. Blow down/Waste Water Evaporation Unit

2.2 Scope of Vendor for Cooling Tower and Associated Packages (ME-444-001, ME-444-002, ME-444-003) Scope of supply includes, but not be limited to the following major equipment and instrumentation as shown on the UFD within the package boundary limit.

2.2.1 Cooling Tower (CT-444-001) Cooling Tower (CT-444-001) to be provided based on the attached datasheet (Attachment1) to be complete with:

- Cooling tower basin divided into two separate divisions, complete with dual strainers/screens and lifting equipment or similar apparatus for screen lifting/cleaning, screens with a lip at the bottom of the frame to catch debris when screens are removed for cleaning









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- Cooling Tower internals, structure, piping, valves and fittings, instrumentation, electrical equipment and control.

- Cooling tower two speed fans. Vendor to specify number of cells and number of fans per cell.

- res.

2.2.2 Cooling Tower Chemical Package (ME-444-002) Cooling Tower Chemical Package (ME-444-002) to be complete with:

- Biocide (sodium hypochlorite) injection system.

- Anti-Scalant injection system .

- Corrosion Inhibition injection system.

Each injection system shall include .

- Two chemical metering pumps for each chemical.

- Chemicals day tanks.

- Air Mask with 30 minute tank

- Chemical package skid internals, structure, piping, valves and fittings, instrumentation, electrical equipment and control.

- .

2.2.3 Cooling Tower Filter Package (ME-444-003) Cooling Tower Filter Package (ME-444-003) to be complete with:

- Two(2) 100% filter vessels (F-444-001).

- Nozzle, Header and Lateral design for service and filter backwash.

- Filter vessels skid internals, structure, piping, valves and fittings, instrumentations including pressure relief devices, electrical and control.

Notes:

1. Filteration rate is 3% of the cooling tower supply flow to users. Vendor is to confirm that filteration rate is sufficient for efficient cooling tower operation.

2. Filter vessels are to be rated for design pressure corresponding to cooling tower pumps shut off heads and design temperature of 60oc. Pumps shut off head is to be confirmed in detail engineering.

3 CODES AND STANDARDS

The packages shall be designed in accordance with the datasheet, job specifications, IPS codes with applicable sections of the latest edition, plus addenda of the codes and









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standards as detailed in Section 3.1 & 3.2. The document order of precedence shall be determined as follows, unless agreed to by Company and/or Contractor:

A) Data sheets.

B) Job specification.

C) Specifications/ CODES mentioned in Section 3.1 & 3.2.

3.1 Job Specifications

The following job specifications and codes shall be used.

SP-38687901-49-001 Water Cooling Tower

SP-38687901-42-001 Towers, Reactors, Pressure Vessels and Internals

SP-38687901-60-002 Electrical Requirements for Packaged Units

SP-38687901-60-001 Three-Phase Squirrel-Cage Induction Motors

SP-38687901-70-130 Instrumentation for Packaged Equipment

SP-38687901-80-002 Painting

SP-38687901-90-001 Site Conditions for Bidboland Gas Treating Plant and Mahshahr Loading Facility

3.2 IPS Specification

IPS-C-PI-240 Construction Standard for Plant Piping System

IPS-C-PI-350 Plant Piping System Pressure Testing

IPS-G-ME-160 Engineering and Material Standard for Water Cooling Towers

IPS-E-PR-790 Engineering Standard for Process Design of Cooling Towers

IPS-E-SF-880 Engineering Standard for Water Pollution Control

IPS-E-PR-491 Engineering Standard for Process Requirements of Refinery Non-Licensed Units

IPS-E-PR-830 Engineering Standard for Process Design of Valves & Control Valves

IPS-E-TP-350 Engineering Standard for Linings

IPS-E-TP-760 Engineering Standard for Corrosion Consideration in Design

IPS-E-TP-780 Engineering Standard for Chemical Control of Corrosive Environments

IPS-E-PR-730 Engineering Standard for Process Design Plant Waste-Water Treatment and Recovery Systems









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IPS-E-EL-100 Engineering Standard for Electrical System Design (Industrial and Non-Industrial)

IPS-E-PR-310 Engineering Standard for Process Design of Water Systems

IPS-E-PI-200 Engineering Standard for Flexibility Analysis

IPS-E-PI-221.1 Engineering Standard for Piping Material Selection.

IPS-E-PI-240 Engineering Standard for Plant Piping System

IPS-E-PR-308 Engineering Standard for Numbering System (Modified by Engineering Standard for Numbering System SP-38687901-00-001).

IPS-E-GN-100 Engineering Standard for Units (Modified by Units of Measurement SP-38687901-00-001)

IPS-E-PR-170 Engineering Standard for Process Flow Diagram

IPS-E-PR-230 Engineering Standard for Piping & Instrumentation Diagrams (P & IDs)









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4 SUPPLY DESCRIPTION

4.1 Process Description

(See Attachment 4; Utility Flow Diagram – BB2-444-0205-1/1)

Cooling water return from users at 49 oC is required to be cooled to 34.5 oC by the cooling tower. Make-up water to the cooling tower is a mixture of several streams as shown on the utility flow diagram. In practice, make-up water may have a variable quality depending on the different streams flow rate ratio and composition resulting in the cooling tower make-up calcium content to vary from an average value. Cooling tower cycle and blowdown is then controlled by the cooling water calcium content. The proper operation of the cooling tower, cycle, and blowdown is achieved and controlled manually by the analysis of the calcium content of the cooling water composite samples. Anti-scalant is added to the cooling water for partial control of calcium deposition. Blow down flow as set by the operator is complementary to anti-scalant injection for calcium control. The conductivity meter provides an alarm if the ion content of the cooling water increases to a high level due to insufficient blow down. The conductivity meter will not be used for direct blowdown control due to the potential variability of the make-water composition and as it is not directly proportional to the calcium content. Cooling tower water is required to be protected against corrosion, scale and biological activities. Cooling tower filter backwash will flow to the evaporator package for water recovery. The cooling tower basin drain is also to be sent to the evaporator package if hydraulic allows. Otherwise it will be sent to the evaporation pond. Detail engineering has to evaluate the hydraulic feasibility of draining the basin water to the evaporator pond considering the elevation difference and plot plan locations of the cooling tower and the evaporator pond.

4.2 Feed Water Condition and Composition

Refer to Attachment 1 for the typical package feed water conditions and composition (Base case). As the exact make-up water to the package may have a variable quality depending on the different streams flow rate ratio and composition that are mixed (See UFD), cooling tower performance and design has to be evaluated and verified for an alternative composition in addition to the typical composition noted as Base Case. Refer to Alternate case for the extreme case of package make-up water composition in Attachment 1 datasheet. Vendor is requested to specify cooling tower blow down rate and associated blow down water quality for both the Base Case and the Alternative Case compositions as per Attachment 1 datasheet.









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4.3 Product Water Specification Refer to Attachment 1 for the required cooling water return conditions and composition.

4.4 Chemical Specification

Vendor is to provide specification for all the chemicals, chemical injection philosophy and operating procedures.

4.5 Design Considerations As discussed above make-up water to the cooling tower is a mixture of several streams and may have variable calcium. Cooling tower cycle and blowdown is then controlled manually. It is important to facilitate this manual control by incorporation of a conservative cooling tower basin design to moderate the variation in the event of the failure of anti-scalant/corrosion inhibitor. It is therefore a good practice depending upon total system volume and blow down rates, to have a deeper basin than required on an equipment mechanical basis alone. Operators set the flow rate of the anti-scalant/corrosion inhibitor to get for example 10 ppm in cooling water. It is desired to have at least 12 hours before the concentration falls by 50% if chemical feeds stop. Otherwise, it will be difficult for the operators to control the cooling tower water quality. Hence, a deeper basin is to be designed to provide sufficient residence time. Vendor is requested to confirm the above operating and control strategy and ensure an efficient design for an operator friendly operation. Minimum recorded temperature being -2ºC may necessitate some mechanism of de-icing. Vendor is to evaluate and recommend whether fans with a low speed reverse for de-icing is to be considered. It is to be noted that the cooling tower design is to be a robust design employing the cross-flow scheme. The cooling tower fill should be splash type. Access to the cooling tower hot well basins is suggested to be left open and not enclosed to keep out the sunlight. Proper chlorination will mitigate potential algae growth in the presence of sunlight. Closing in the hot wells makes their routine inspection a confined space and potentially will limit the routine inspections.









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5 GENERAL

5.1 Location

Bid Boland Gas Treating Plant No II is located at the South west part of Iran, about 15 km North West of Behbahan city in Khuzestan province.

5.2 Utilities

The following utilities are available:

5.2.1 Cooling Medium

• Water Cooling

Supply temperature = 34.5°C Maximum water return temperature = 49°C Minimum process temperature after water cooling = 40°C Supply / Return pressure, bar(g) = 8.0 / 6.5 (to be verified)

• Air Cooling

Air temperature for design is 48°C.

The minimum temperature to which process fluids can be cooled using air cooling is 58°C considering 10°C approach.

Air cooling is preferred to water cooling where possible.

5.2.2 Heating Medium The following utilities are available:

LP Steam: Low pressure steam at 4.5 bar(g).

De-superheating medium available : HP condensate with following condition: Header Supply Pressure, bar(g) 9.3 Header Supply Temperature , °C 181

Let down valve will be installed by EPC to the required pressure.

5.2.3 Cold Condensate Supply Pressure, bar(g) 12 Supply Temperature , °C 65

5.2.4 Nitrogen System Nitrogen gas is available.

Nitrogen header operating pressure : 5.0 bar(g) @ 40°C.









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Design 11.5 bar(g) @ 86°C based on Nitrogen receiver pressure.

Oxygen shall be minimum to meet Vendor’s requirements. Nitrogen purity is 99.5%.

5.2.5 Instrument Air / Plant Air

Instrument Air receiver is operating at 8 barg and 40°C (dried).

5.2.6 Electric Power

The following electricity is available on site:

Up to 0.25 kW 230V-1PH-50 Hz

0.251 to 150 kW 400V-3PH-50 Hz

151 to 2500 kW 6.0 kV-3PH-50 Hz

5.3 Site Data

Site data as presented here, are extracted from Document # SP-38687901-90-001 Rev 0 “Site Conditions for Bid Boland Gas Treating Plant II”.

5.3.1 Plot Plan

See Attachment 5 : Overall Plot Plan.

5.3.2 Design life

Plant to be designed for 25 years life.

5.3.3 Environmental condition

Altitude is approximately 325 m above sea level. Atmosphere is semi-arid, saliferous and dusty with occasional sand storms and periods of high humidity.

(1) Temperature and Humidity

Maximum recorded temperature : 52ºC Minimum recorded temperature : -2ºC Winterizing temperature : not required Wet bulb temperature (design) : 29ºC Dry bulb temperature (design) : 48ºC Max. temp. for mechanical, civil and structural design : 55ºC Equipment exposed to sunlight : 86ºC Soil temp. for cable selection: 30ºC Design temp. for air cooler, dry : 48ºC Design temp. for air blower, dry : 48ºC Maximum relative humidity 80% @ 23ºC Minimum relative humidity : 11% Design relative humidity : 25% @ 48ºC









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(2) Solar Radiation

0.7883 kW/m2 (250 BTU / hr x ft 2 ).

(3) Barometric Design Pressure

0.980 bara.

(4) Wind Data

Design wind velocity : 140 Km/hr Prevailing wind direction : North – West

(5) Rainfall

Maximum in one hour :40 mm Design snow load : Not to be considered. Rainfall value for sewer design : 40 mm/hr

Winter rainfall may vary from nil to 20 inches per season. The rainfall may occur as tropical storms.

(6) Sandstorms

Occasional.

(7) Thunder and Lightning

To be considered. (8) Earthquake

Earthquake shall be considered for Zone 3 as per Uniform Building Code (UBC).

6 BASIC ENGINEERING REQUIREMENTS

6.1 General

The Vendor shall determine a design that meets the guaranteed statements as specified in Section 4.

The Process Vendor, in close co-operation with ENGINEERING CONTRACTOR, with regards to process design, equipment constructability, transportation and erection as well as plant operation reliability and availability shall optimise the process flow diagram.

Process Vendor responsibility is limited to the items within the Unit Battery Limits. However, the general arrangement of the whole Plant shall be taken into consideration for all scheduled Project Concept.









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6.2 Equipment Design Requirements

All equipment design shall follow generally accepted international standards and Vendor own requirements, according to Vendor’s know-how. Compatibility with Iranian Petroleum Standards (IPS) shall be checked by EPC and any potential conflict shall be brought to the attention of Vendor for resolution. Relevant IPS Standards are listed in Section 3.

6.3 Turndown Ratio Design for 40% turn down ratio as minimum.

Vendor to advise if the lower turndown is possible.

6.4 Design Margin All rotating equipment shall have 10% design margin in flow.

Chemical injection pumps shall have 20% design margin in flow.

6.5 Heat Exchanger Design The following approach temperatures shall be followed during the design of heat

exchangers:

10°C for Air Coolers

5.5°C for Shell and Tube Heat Exchangers

2.8°C for Plate and Frame Exchangers

6.6 Vessel Design

Pressure vessels shall be designed as per ASME Section VIII Div 1, unless otherwise specified in SP-38687901-42-001.

6.7 Piping Design and Layout

Plant piping design, class identification shall be as per IPS. Vendor shall be responsible for line sizing and assigning piping classes (as provided by EPC) and material selection.

6.8 Metallurgy

All material shall be designed in accordance with recognized international codes and standard and vendor know – how. As a minimum the following allowances for corrosion and / or mechanical strength shall be used for carbon steel piping and equipment.

For piping material selection: IPS E-PI-221 Parts 1, 2 and 3 "Piping Material Selection, On-Plot Piping" For vessels and equipment: IPS E-TP-740 "Corrosion Considerations in Materials Selection" and IPS E-TP-760 "Corrosive Consideration in Design".









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6.9 Chemical and Catalysts

To be indicated by Vendor.

6.10 Effluents

To be indicated by Vendor.

6.11 Operation

6.11.1 Operational Requirements (1) Criticality and Availability

(2) Operating, Maintenance and Control Provisions

Guidelines to be provided by Vendor.









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7 OTHER REQUIREMENTS

(1) Vendor Data Requirements

Vendor will provide the following: • Process Description • Operating Manual • Process Flow Diagram with Heat and Mass Balance • Piping & Instrumentation Diagrams (P& IDs) • Process Equipment data sheets with material requirements (or Design

data) for all equipment • List of Chemicals and Consumption • List of utilities and consumption • Tank storage requirements for chemicals • Cause and Effect Diagrams • Alarm and Set points • Instrument datasheets • Control valve process datasheet • PSV Datasheets • On/Off valve process datasheet • List of Laboratory Analysis Method, chemicals and apparatus • Material Safety Data Sheets for unit’s chemicals • List of emissions with amounts • Unit Control philosophy and description • Proposed Plot Plan • Skid dimensions and total space requirement, including free space for

maintenance access. • Recommended Spare Parts List/Consumables Other data:

- Cooling Tower Design and Calculation

- General arrangement drawings

- Cooling Tower and all internal components detail drawings

- Performance projection and guarantees

- Blow down specifications and procedures

• Operating, control, and shutdown philosophies and procedure Corrosion inhibition/Biocide/Anti-Scalant plans and procedure . .

• Chemical injection philosophy and operating procedures

(3) Unit and Equipment Tags

EPC will provide the new equipment tags.

8 REFERENCE DOCUMENTS









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Reference documents as per Datasheets, per Section 3 of this document, Utility Flow Diagram

9 UNITS OF MEASUREMENTS (Reference: Document SP-38687901-00-001 Rev 0)

Property Unit Property Unit Acidity mg KOH/g Emissions mg/mile Act. Gas Flow ACT_m3/h Energy kcal/h Act. Vol. Flow m3/h Energy (Lrg) cal Actual Liquid Flow m3/s Enth. Coeff. CA kJ/kg Actual Mass Density kg/m3 Enth. Coeff. CB kJ/kg-K Area m2 Enth. Coeff. CC kJ/kg-K^2 AreaPerVolume m2/m3 Enth. Coeff. CD kJ/kg-K^3 BWR 'Alpha' m9/mol3 Enth. Coeff. CE kJ/kg-K^4 BWR 'B' m6/mol2 Enth. Coeff. CF kJ/kg-K^5 BWR 'B0' m3/mol Enthalpy Per Length kJ/h-m BWR 'C' bar m9 K2/mol3 Entropy kJ/kgmole-C BWR 'C0' bar m6 K2/mol2 Flow kgmole/h BWR 'A' bar m9/mol3 Force newton BWR 'A0' bar m6/mol2 Fouling C-h-m2/kcal Cake Loading m/kg Frequency rpm Comp. Mass Flow kg/h Friction Power Loss Factor kg-m2/s Comp. Mole Flow kgmole/h Fuel Oil eqv Factor teFOE/te Comp. Vol. Flow m3/h Fuel Oil eqv Mass Flowrate teFOE/h Compressibility 1/bar Gas Oil Ratio m3/m3 Concentration % Gibbs. Coeff. CA kJ/kgmole Cost Index Cost Gibbs. Coeff. CB kJ/kgmole-K Cost Index per Energy Cost/kcal Gibbs. Coeff. CC kJ/kgmol-K^2 Cost Index per Time Cost/s Heat Capacity kJ/kgmole-C Cost Per FOE Cost/kgmole Heat Flux kJ/h-m2 Cost Per Mass Cost/kg Heat Of Vap. kcal/kgmole Cost Per Mole Cost/teFOE Heating Value kcal/kgmole Cost Per Volume Cost/m3 Ht. Tran. Coeff kcal/h-m2-C Deactivation Rate C/(bbl/lb) Kinematic Visc. cSt Delta Pressure bar Large Heat Flow kcal/h Delta Temp. C Lead Level in Gasoline kgPb/m3 Diffusivity m2/s Length m Dynamics Cv USGPM Liq. Vol. Flow m3/h Dynamics k - Laminar sqrt(kg/s/(kPa-

kg/m3)) Mass kg

Dynamics k - Turbulent kg/hr/sqrt(bar-kg/m3) Mass Concentration wt % Electric Potential V Mass Concentration ppm ppmwt Electrical Conductivity S/m Mass Cp kJ/kg-C Electrical Flow kW-h/h Mass Density kg/m3 Electrical Fuel Oil Factor teFOE/kW-h Mass Enthalpy kcal/kg Mass Enthalpy Flow kJ/kg-s Rho-V-Sqr kg/m-s2 Mass Entropy kJ/kg-C Rotational Inertia kg-m2 Mass Flow kg/h SG Unitless Mass Heat Of Vap. kcal/kg SG Air rel_to_air









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Property Unit Property Unit Mass Heating Value kcal/kg Small Area mm2 Mass Ratio Concentration wt/wt Small Length mm Mass Reaction Rate kgmol/kg-s Specific Volume m3/kg Mass Transfer Coefficient kgmol/m2-s-Pa Standard Density kg/m3 Mass Velocity kg/s-m2 Std. Gas Flow STD_m3/h Mass Yield From Reaction kg/kg Std. Vol. Flow m3/h Molar Concentration mol % Steam Ratio kgsteam/m3 Molar Concentration ppm ppmmol Surf Tension dyne/cm Molar Density kgmole/m3 Surge Control Parameter A m Molar Electrical Conductivity S-m2/kgmole Surge Control Parameter B m/(m6/s2) Molar Enthalpy kcal/kgmole Temperature C Molar Ratio Concentration mol/mol Thermal Cond. kcal/h-m-C Molar Volume m3/kgmole Time seconds Molar Yield From Reaction kgmol/kg UA kcal/h-C Moles kgmole Unitless Unitless Moles Per Mass kgmol/kg Valve CV Mass kg/h-kPa Oil Volume m3 Valve CV Mole kgmole/h-kPa Per Mass Volume per kg-m3 Valve CV Volume m3/h-kPa Per Volume per m3 Vapour Fraction Unitless Percent % Vapour Volume nm3 Permeability m3/s2 Velocity m/s Power kW VFlowPerArea m3/h-m2 Power Per Flow kW/kgmole/s VFlowPerLength m3/h-m PressPerLength kPa/m Viscosity cP Pressure bar Volume m3 Quick Opening Rate %/s Volume Concentration vol % Reaction Rate kgmole/m3-s Volume Concentration ppm ppmvol Reciprocal FOE 1/teFOE Volume Ratio nm3/m3 Reciprocal Mass 1/kg Volume Ratio Concentration vol/vol Reciprocal Moles 1/kgmole Volume Specific Energy MJ/m3 Reciprocal Time 1/seconds Volumetric Enthalpy Flow kJ/m3-s Reciprocal Vapour Volume 1/nm3 Work kW Additional:

Gas flow rate, DCS display MMSCFD Liquid mass flow rate, DCS display

T/D (Tonnes/day)

Gas Flow rate, Design doc Kg/hr Weight T (tonnes)

Gas Flow rate, Design doc Nm3/hr Numbers to be expressed as 1,000 or 1,000,000.









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10 ATTACHMENTS Attachment 1 Cooling Tower Datasheet Attachment 2 Cooling Tower Chemical Package Datasheet Attachment 3 Cooling Tower Filter Package Datasheet Attachment 4 Utility Flow Diagram- BB2-444-0205 Rev.4 Attachment 5 Overall Plot Plan

Documents

Data sheet for cooling Tower