1
Any opinions, findings, and conclusions or recommendations expressed in this material are those of the authors and do not necessarily reflect the views of the FAA or other ASCENT Sponsors. Project #ASCENT COE-2014-01 Techno-Economic Evaluation of Sustainable Jet Fuel Conversion Processes: The Alcohol-to-Jet Process Scott Geleynse, Kristin Brandt, Xiao Zhang*, Manuel Garcia-Perez, Michael Wolcott Lead investigator: M. Wolcott, M. Garcia-Perez, X. Zhang Washington State University Project manager: Nathan Brown, FAA September 26-27, 2017 Summary There are several strategies currently under investigation by commercial entities for the production of alcohols for use in ATJ conversion. Although higher alcohols provide greater yield and efficiency in the catalytic upgrading steps, they face trade-offs in the form of lower fermentation yield and higher production costs. In addition, the type of intermediate alcohols used will impact the final hydrocarbon distribution and fuel properties. Results and Discussion Comparisons between ethanol and isobutanol-based ATJ conversion processes using fermentation are shown below. Ethanol fermentation is an established technology, while isobutanol fermentation requires proprietary engineered biocatalyst. Two isobutanol fermentation scenarios are compared: one with expenses equal to ethanol fermentation, and one with double capital and variable operating costs. Even in the high-cost scenario, isobutanol fermentation offers a lower conversion cost (minimum fuel selling price) over ethanol fermentation. Comparison of Upgrading Costs of Ethanol and Isobutanol: Motivation and Objectives Alcohol-to-jet (ATJ) is a process for the upgrading of alcohols to an alternative jet fuel. With the potential to generate these alcohols from biorenewable resources, this pathway provides a means for producing a sustainable alternative jet fuel (SAJF). This process has been under development by several organizations and is the subject of recent updates to the current ASTM standards for commercial jet fuel. With the large installed capacity of domestic alcohol production, ATJ may offer a near-future opportunity for renewable alcohols to enter the market for drop-in aviation biofuels. ATJ is a flexible process capable of generating a range of fuel products and commodity chemicals in addition to jet fuel, and is based on several catalytic steps historically utilized by the petrochemical industry. Process simulation and economic modeling is employed to assess some varying implementations of ATJ conversion schemes. Methods Process models for ATJ conversion were constructed based on data from literature and generated using Aspen Plus simulation software. Capital and operating expenses were estimated for both standalone “Core ATJ” units to upgrade alcohols as well as “Full ATJ” facilities to process generic sugar streams into SAJF. These models were constructed for both the use of ethanol as an intermediate as well as a higher alcohol (isobutanol), to compare the contrasting advantages of the direct production of higher alcohols over more conventional fermentation processes. 1. Alcohol-to-Jet conversion technology provides a flexible platform for SAJF conversion that can utilize existing alcohol production capacity and generate a variety of fuels. 2. A need for further research and development of higher-alcohol production technologies to improve process economics in ATJ conversion is identified. 3. Techno-economic process models with standardized assumptions and methods are shown to be useful for comparison of SAJF pathways. Further application of this modularized approach is recommended to continue comparing conversion strategies. 4. Co-product generation technologies may be necessary to identify and compare viable SAJF pathways. A “Road-Map” of ATJ Conversion and Co-Product Opportunities: Objectives: Apply new standardized ASCENT methodology to generate process and economic data of ATJ for comparison with other technologies Compare alternative implementation strategies of ATJ conversion Identify areas requiring further research, and potential co-products to improve process economics The minimum selling price (MSP) of jet fuel produced from ethanol and isobutanol, as a function of alcohol production price, illustrates the cost benefits of higher alcohol production. An isobutanol production cost of 1.68 times the cost of ethanol results in equal selling prices. Chemistry of the “Core ATJ” Process: Catalytic Upgrading of Alcohols to Paraffins Conclusions and Next Steps Careful selection of alcohol intermediates is a key to the successful implementation of an ATJ conversion process. Efficient utilization of available low-cost feedstock (gas or sugar) and existing process infrastructure provides cost-reduction opportunities. The production of higher alcohols through direct production or additional upgrading stages provides opportunities to improve process costs downstream as well as the potential for co-product generation that may greatly improve commercial viability. This “road-map” (left) illustrates potential process schemes and co-products. Alcohol-Producing Process Companies and Institutions Interested/Inv ested in Technology Alcohol Intermediate Expected Hydrocarbon Product Distribution Gevo Integrated Fermentation Technoloy (GIFT®) Process Gevo iso-butanol C8, C12, C16 branched N-butanol Fermentation (via ABE fermentation or other) Cobalt, Butamax n-butanol C8, C12, C16 unbranched Ethanol Fermentation Byogy Ethanol C4-C12 unbranched Gas (CO, syngas) Fermentation Lanzatech, PNNL Ethanol C4-C16 range unbranched Catalytic (thermochemical) Conversion of Syngas to Ethanol PNNL Ethanol C4-C16 range unbranched Comparison of Alcohol Producing Strategies for ATJ Conversion: $0.00 $2.00 $4.00 $6.00 $8.00 $10.00 $12.00 $0 $200 $400 $600 $800 $1,000 $1,200 $1,400 $1,600 MSP ($/gal) Alcohol Price ($/ton) Ethanol Isobutanol Ethanol Conversion Isobutanol Conversion (low cost) Isobutanol Conversion (high cost) Overall Mass Yield 0.230 0.276 0.276 Alcohols Processed (ton/day) 200 161 161 Total Capital Investment, MM$ $82.60 $54.91 $94.17 OpEx, MM$/yr $16.8 $13.9 $18.4 Production Rate, MMgal/yr 9.85 11.83 11.83 Cost per ton sugar $188.43 $145.48 $209.33 Conversion Cost, $/gallon fuel $2.734 $1.757 $2.528 Avg. cost of ethanol production Acknowledgements This work was funded by the US Federal Aviation Administration (FAA) Office of Environment and Energy as a part of ASCENT Project 01 under FAA Award Number: [ 13 - C - AJFE - WASU ASCENT project COE - 2014 - 01] and an Agriculture and Food Research Initiative Competitive Grant No. 2011-68005-30416 from the USDA National Institute of Food and Agriculture. We thank Drs. Karthi Ramasamy and Rich Hallen from Pacific Northwest National Laboratory (PNNL) for discussion and suggestions.

Project #ASCENT COE-2014-01 Techno-Economic Evaluation of

  • Upload
    others

  • View
    0

  • Download
    0

Embed Size (px)

Citation preview

Page 1: Project #ASCENT COE-2014-01 Techno-Economic Evaluation of

Any opinions, findings, and conclusions or recommendations expressed in this material are those of the authors and do not necessarily reflect the views of the FAA or other ASCENT Sponsors.

Project #ASCENT COE-2014-01

Techno-Economic Evaluation of Sustainable Jet Fuel Conversion Processes: The Alcohol-to-Jet Process

Scott Geleynse, Kristin Brandt, Xiao Zhang*, Manuel Garcia-Perez, Michael Wolcott

Lead investigator: M. Wolcott, M. Garcia-Perez, X. ZhangWashington State University

Project manager: Nathan Brown, FAASeptember 26-27, 2017

Summary

There are several strategies currently under investigation by commercial entitiesfor the production of alcohols for use in ATJ conversion. Although higher alcoholsprovide greater yield and efficiency in the catalytic upgrading steps, they facetrade-offs in the form of lower fermentation yield and higher production costs. Inaddition, the type of intermediate alcohols used will impact the final hydrocarbondistribution and fuel properties.

Results and Discussion

Comparisons between ethanol and isobutanol-based ATJ conversion processesusing fermentation are shown below. Ethanol fermentation is an establishedtechnology, while isobutanol fermentation requires proprietary engineeredbiocatalyst. Two isobutanol fermentation scenarios are compared: one withexpenses equal to ethanol fermentation, and one with double capital and variableoperating costs. Even in the high-cost scenario, isobutanol fermentation offers alower conversion cost (minimum fuel selling price) over ethanol fermentation.

Comparison of Upgrading Costs of Ethanol and Isobutanol:

Motivation and Objectives

Alcohol-to-jet (ATJ) is a process for the upgrading of alcoholsto an alternative jet fuel. With the potential to generate thesealcohols from biorenewable resources, this pathway provides ameans for producing a sustainable alternative jet fuel (SAJF).This process has been under development by severalorganizations and is the subject of recent updates to thecurrent ASTM standards for commercial jet fuel. With the largeinstalled capacity of domestic alcohol production, ATJ mayoffer a near-future opportunity for renewable alcohols to enterthe market for drop-in aviation biofuels. ATJ is a flexibleprocess capable of generating a range of fuel products andcommodity chemicals in addition to jet fuel, and is based onseveral catalytic steps historically utilized by the petrochemicalindustry. Process simulation and economic modeling isemployed to assess some varying implementations of ATJconversion schemes.

Methods

Process models for ATJ conversion were constructed basedon data from literature and generated using Aspen Plussimulation software. Capital and operating expenses wereestimated for both standalone “Core ATJ” units to upgradealcohols as well as “Full ATJ” facilities to process genericsugar streams into SAJF. These models were constructed forboth the use of ethanol as an intermediate as well as ahigher alcohol (isobutanol), to compare the contrastingadvantages of the direct production of higher alcohols overmore conventional fermentation processes.

1. Alcohol-to-Jet conversion technology provides a flexible platform for SAJFconversion that can utilize existing alcohol production capacity andgenerate a variety of fuels.

2. A need for further research and development of higher-alcoholproduction technologies to improve process economics in ATJ conversionis identified.

3. Techno-economic process models with standardized assumptions andmethods are shown to be useful for comparison of SAJF pathways.Further application of this modularized approach is recommended tocontinue comparing conversion strategies.

4. Co-product generation technologies may be necessary to identify andcompare viable SAJF pathways.

A “Road-Map” of ATJ Conversion and Co-Product Opportunities:

Objectives:

•Apply new standardized ASCENT methodology togenerate process and economic data of ATJ forcomparison with other technologies

•Compare alternative implementation strategies of ATJconversion

•Identify areas requiring further research, andpotential co-products to improve process economics The minimum selling price (MSP) of jet fuel produced from ethanol and

isobutanol, as a function of alcohol production price, illustrates the costbenefits of higher alcohol production. An isobutanol production cost of 1.68times the cost of ethanol results in equal selling prices.

Chemistry of the “Core ATJ” Process: Catalytic Upgrading of Alcohols to Paraffins

Conclusions and Next Steps

Careful selection of alcoholintermediates is a key to thesuccessful implementation of anATJ conversion process. Efficientutilization of available low-costfeedstock (gas or sugar) andexisting process infrastructureprovides cost-reductionopportunities. The production ofhigher alcohols through directproduction or additionalupgrading stages providesopportunities to improve processcosts downstream as well as thepotential for co-productgeneration that may greatlyimprove commercial viability. This“road-map” (left) illustratespotential process schemes andco-products.

Alcohol-Producing Process

Companies and Institutions Interested/Invested in Technology

Alcohol Intermediate

Expected Hydrocarbon Product Distribution

Gevo Integrated Fermentation Technoloy (GIFT®) Process

Gevo iso-butanol C8, C12, C16 branched

N-butanol Fermentation(via ABE fermentation or other)

Cobalt, Butamax n-butanol C8, C12, C16 unbranched

Ethanol Fermentation Byogy Ethanol C4-C12 unbranched

Gas (CO, syngas) Fermentation

Lanzatech, PNNL Ethanol C4-C16 range unbranched

Catalytic (thermochemical) Conversion of Syngas to Ethanol

PNNL Ethanol C4-C16 range unbranched

Comparison of Alcohol Producing Strategies for ATJ Conversion:

$0.00

$2.00

$4.00

$6.00

$8.00

$10.00

$12.00

$0 $200 $400 $600 $800 $1,000 $1,200 $1,400 $1,600

MSP ($/gal)

Alcohol Price ($/ton)

Ethanol Isobutanol

Ethanol Conversion Isobutanol Conversion (low cost)

Isobutanol Conversion (high cost)

Overall Mass Yield 0.230 0.276 0.276

Alcohols Processed

(ton/day)

200 161 161

Total Capital Investment,

MM$

$82.60 $54.91 $94.17

OpEx, MM$/yr $16.8 $13.9 $18.4

Production Rate, MMgal/yr 9.85 11.83 11.83

Cost per ton sugar $188.43 $145.48 $209.33

Conversion Cost, $/gallon

fuel

$2.734 $1.757 $2.528

Avg. cost of ethanol production

Acknowledgements

This work was funded by the US Federal Aviation Administration (FAA) Office ofEnvironment and Energy as a part of ASCENT Project 01 under FAA AwardNumber: [13-C-AJFE-WASU ASCENT project COE-2014-01] and an Agricultureand Food Research Initiative Competitive Grant No. 2011-68005-30416 from theUSDA National Institute of Food and Agriculture.We thank Drs. Karthi Ramasamy and Rich Hallen from Pacific Northwest NationalLaboratory (PNNL) for discussion and suggestions.