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Making our planet more productive Enhanced Biomass-to-Liquids Project Development and Modeling S. Chakravarti, D. P. Bonaquist, R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda, NY Prepared for presentation at FOCAPO 2012 Savannah, GA

Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Page 1: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

Making our planet more productive

Enhanced Biomass-to-Liquids –

Project Development and Modeling

S. Chakravarti, D. P. Bonaquist,

R. F. Drnevich and M. M. Shah

Praxair Technology, Inc.

Tonawanda, NY

Prepared for presentation at

FOCAPO – 2012

Savannah, GA

Page 2: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productiveOutline

Biomass-to-Liquids

Modeling Approach for Project Development

Key Modeling Issues

Practical Considerations in Project Development

Vision of Better Modeling Tools

Page 3: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productive

Drivers

Domestic energy

independence

Lower CO2 footprint

Tax credits

Significant project

development activity

Market

Cap for

1st Gen

Biofuels

2nd Gen

Biofuels

912 13 14 15 15 15 15

2008 2010 2012 2014 2016 2018 2020 2022

36

30

26

22

1815

13

9

Renewable Fuels Standard Requirements

(Billion Gallon Ethanol Equivalents)

Source: Energy Independence and Security Act of 2007

1st Gen – Corn ethanol

2nd Gen – Ethanol, diesel from non-food sources

Page 4: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productiveNext Generation Biofuels:

Different Pathways Bring Different Opportunities

Sugars

Energy crops

Agricultural residue

Woody biomass

MSWPyrolysis and/or

Gasification

Alcohols,

Organic Acids,

& Hydrocarbons

O2

H2

CO2

Biochemical

H2

Fermentation or

Digestion

Thermochemical

Algae Renewable DieselOil Extraction &

Hydroprocessingfor algae growth

H2

N2

Near

term

Hydroprocessing

Vegetable oils

Animal fats

Algal lipids

Hydrocarbons,

Renewable DieselH2

N2

Today

Long

term

Gasification offers better potential for near-term commercialization

Issue: Limited feedstock supply

Page 5: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productiveBiomass to Liquids – Baseline

Low biofuel yield significantly impacts economic viability

Gasification +

ReformingConditioning

Catalytic

ConversionBiomass

900 dry

tons/day

O2

350 tpd

Syngas FT Liquids*

1125 BBL/d

Non-gasification approaches are also under development.

Technical /Economic Viability Uncertain

Needs demonstration on commercial scale

Gasification, Catalytic Methanol/MTG / Fischer-Tropsch liquids

Commercial Technologies

* 75% diesel, 25% naphtha

* Adapted from “Wood to Wheels –The Challenges of Large Scale Forest Biomass to Liquids Conversion”,

R. Holford, International Biomass Conference, St. Louis, May 3rd 2011.

Page 6: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productiveEnhanced Biomass-to-Liquids*

Maximizes yield with addition of H2-rich syngas

Yield increase limited by lifecycle GHG emission constraint

Increases overall system availability

Enables start-up with SMR versus gasifier

No need for a startup boiler

Improves economies of scale for syngas to liquids section

~2.5X Yield versus straight Biomass to FT Liquids

Gasification +

ReformingConditioning

Catalytic

Conversion

Biomass

900 dry

tons/day

Syngas FT Liquids*

2650 BBL/d

SMR

NG

NG-derived

syngas

* 75% diesel, 25% naphtha

Tail Gas

* US Patent Application 2011/0218254 A1

O2

350 tpd

Page 7: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productiveComparison of Biofuel Production

Pathways*

*Adapted from “Techno-economic comparison of biomass-to-transportation fuels via pyrolysis,

gasification and biochemical pathways”, Anex RP et al., Fuel (2010)

Potential for additional

30% increase

Praxair’s technology significantly increases yield of gasification pathway

0

25

50

75

100

125

Biochemical (dilute acid,

base case)

Biochemical (dilute acid,

high solids)

Pyrolysis (internal H2

production)

Pyrolysis (external H2)

Gasification (low

temperature)

Gasification (high

temperature)

Gasification (with Praxair

technology)

Gal

lon

s B

iofu

el /

To

n B

iom

ass

Page 8: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productiveProject Development / Analysis

Site selection

Biomass feedstock definition

Product slate definition

Process/system design

Heat and material balance

Utility and emissions

Estimation of lifecycle GHG

emissions

Vendor quotes for sub-systems

Cost estimation

Feedstock and product pricing

forecasts

Project Economics

Business Planning

Project risk assessment

EPC contractor interfacing

Modeled each item independently and iterated as required to

optimize project

Page 9: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productiveCurrent Modeling Approach

Process /

System

Design

CO2 footprint

< Threshold

Project return

Meets

Criteria?

Yes Yes

No

No

Next

Project

Phase

Adjust

inputs

Feedstock

Type , rate

Product

Cost

Estimating

Financing

OptionsPrice

forecasts

Site

Vendor

quotes

UNISIMGREET

Excel-based

Page 10: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productiveKey Modeling Issues

No common platform

Manual interfaces between

platforms

Variety of inputs – process,

financial, regulatory

Complexity drives use of less

rigorous shortcut methods

Rigor also limited by availability of

sub-system models, e.g.

Gasifier

FT Liquids and Liquids Upgrading

Capital cost estimation

Always a challenge for first-of-a-

kind plants

Mechanism for using vendor

quotes not available

Interpretation of level of accuracy

and adjustment for contingency

requires a tool like the RAND

analysis*

Limited database for costing

software

Need for a unified modeling tool to assist with project

development on a case-by-case basis

* Understanding cost growth and performance shortfalls in pioneer process plants. E. Merrow, K.

Phillips and C. Myers, RAND Corp.; 1981. Report No.: RAND/R-2569-DOE.

Page 11: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productive

Selection Criteria

Site area

Proximity to market

Regional construction productivity

Feedstock availability and pricing

Transportation of feedstock to site

Availability of utilities

Electrical power

Water / wastewater treatment

Natural gas

Potential site synergies

Selected existing industrial facility in Southeastern US

Site

Key factors – Feedstock availability and site synergies

Page 12: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productive

Candidates

Agricultural residue, e.g. corn stover

High energy crops, e.g. switchgrass

Woody biomass, e.g. forest residue, wood chips, wood logs

Municipal Solid Waste

Selection criteria

Cost of feedstock delivered to site

Continuous and abundant supply / no seasonal disruptions

Minimum variability

Infrastructure for collection and transportation

Selected wood chips – 900 tons/day @ $ 60 - $ 80 per bone dry ton

Biomass Feedstock Definition

Feedstock rate constrained by delivered price

Page 13: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productive

Candidates

Methanol / Methanol-to-Gasoline

Ethanol

FT Liquids – Diesel, naphtha, waxes

Selection criteria

Product value

Complexity of product synthesis

Fungibility with existing fuel infrastructure

Forecasted demand and pricing

Selected FT Liquids (diesel, naphtha) – 2650 BBL/d production rate

Product Slate Definition

Production rate limited by lifecycle CO2 emission constraint

Page 14: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productive

Classical flowsheet synthesis

Heat/Material/Utility/Emissions defined for 900 dry ton/day biomass

Multiple process/system configurations evaluated within UNISIM

Air Separation Unit

Feedstock Management

Gasification

Gas Cooling

Acid Gas Removal and Sulfur Management

SMR (Steam Methane Reforming) System

FT Liquids

Liquids Upgrading

Power Generation

Off-sites

Selection criteria

Risk profile

Technology readiness

Ability to bid project immediately

Process/System Design

Page 15: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productiveBlock Flow Diagram

F-T Tail Gas

3. GasificationWood chips

O2

5. Acid Gas Removal

&

Sulfur Management

4. Gas Cooling2. Feedstock

Management

7. FT

Liquids

8. Liquids

Upgrading

Diesel

Naphtha

Syngas

1800oF

6. SMR

System

NG

SMR syngas

Vent or

CO2 plant

Bio-syngas

CO2 to Gasifier

H2

Steam

Sulfur

(as spent adsorbent)

No technology demonstration required –

Selected for next project phase

Novel combination of existing technologies

Optimized facility for yield while satisfying CO2 footprint constraints

1. Air

Separation Unit

9. Power

Generation

10. Off-sites

Page 16: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productive

Estimate reduction in lifecycle greenhouse gas emissions versus

petroleum derived fuels

CO2 footprint

Renewable Fuels Standard

60% reduction in GHG emissions – cellulosic biofuels

50% reduction in GHG emissions – advanced biofuels

Modeling platform – GREET (Greenhouse gases, Regulated

Emissions and Energy use in Transportation) model from Argonne

National Lab

Lifecycle GHG emissions

Cellulosic RIN credits most valuable

Page 17: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productiveMethodology for Capital Cost Estimate

Opportunity to automate process for estimating capital costs

Process /

System

Design

Performance Specifications

by Sub-System

RFPs to Sub-System

Vendors

Select sub-system vendor based on

Cost, performance and technical readiness

Estimate direct costs by sub-system

Adjust for indirect costs –

Engineering, construction management

Add owners’ engineering, contingency

Total Capital Investment

EPC firm

Praxair

Page 18: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productiveProject Economics

Inputs

Capital cost

Production capacity

Availability estimate

Fixed and operating costs

Feedstock and product pricing

forecasts

Financing options

Construction period

Project life

Process performance

Modeling tool

Excel-based DCF model

Outputs

Revenue and OP projections

IRR

Project selection criteria

Risk

Financing considerations

IRR

Compare with crude oil price forecast

Page 19: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productiveCurrent Modeling Approach …

Process /

System

Design

CO2 footprint

< Threshold

Project return

Meets

Criteria?

Yes Yes

No

No

Next

Project

Phase

Adjust

inputs

Feedstock

Type , rate

Product

Cost

Estimating

Financing

OptionsPrice

forecasts

Site

Vendor

quotes

UNISIMGREET

Excel-based

Page 20: Enhanced Biomass-to-Liquids Project Development and Modelingfocapo.cheme.cmu.edu/2012/presentations/Chakravarti.pdf · R. F. Drnevich and M. M. Shah Praxair Technology, Inc. Tonawanda,

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Making our planet more productiveWith Better Modeling Tools

Process /

System

DesignCO2 footprint

< Threshold

Project return

Meets

Criteria?

Next

Project

Phase

Feedstock

Type , rate Product

Cost

Estimate

Site Vendor

quotes

Price

forecasts

Financing

Options

Ultimate objective – Single integrated modeling platform