skip to main content
OSTI.GOV title logo U.S. Department of Energy
Office of Scientific and Technical Information

Title: Techno-Economic Analysis of Biochemical Scenarios for Production of Cellulosic Ethanol

Abstract

A techno-economic analysis on the production of cellulosic ethanol by fermentation was conducted to understand the viability of liquid biofuel production processes within the next 5-8 years. Initially, 35 technologies were reviewed, then a two-step down selection was performed to choose scenarios to be evaluated in a more detailed economic analysis. The lignocellulosic ethanol process was selected because it is well studied and portions of the process have been tested at pilot scales. Seven process variations were selected and examined in detail. Process designs were constrained to public data published in 2007 or earlier, without projecting for future process improvements. Economic analysis was performed for an 'nth plant' (mature technology) to obtain total investment and product value (PV). Sensitivity analysis was performed on PV to assess the impact of variations in process and economic parameters. Results show that the modeled dilute acid pretreatment process without any downstream process variation had the lowest PV of $3.40/gal of ethanol ($5.15/gallon of gasoline equivalent) in 2007 dollars. Sensitivity analysis shows that PV is most sensitive to feedstock and enzyme costs.

Authors:
; ; ; ; ; ;
Publication Date:
Research Org.:
National Renewable Energy Lab. (NREL), Golden, CO (United States)
Sponsoring Org.:
USDOE
OSTI Identifier:
982937
Report Number(s):
NREL/TP-6A2-46588
TRN: US201014%%765
DOE Contract Number:  
AC36-08GO28308
Resource Type:
Technical Report
Country of Publication:
United States
Language:
English
Subject:
09 BIOMASS FUELS; 32 ENERGY CONSERVATION, CONSUMPTION, AND UTILIZATION; 59 BASIC BIOLOGICAL SCIENCES; BIOFUELS; DOLLARS; ECONOMIC ANALYSIS; ECONOMICS; ENZYMES; ETHANOL; FERMENTATION; GASOLINE; PRODUCTION; SENSITIVITY ANALYSIS; VIABILITY; CELLULOSIC ETHANOL; PRODUCT VALUE; BIOCHEMICAL; FEEDSTOCK; ENZYME; PROCESS DESIGN; DILUTE ACID PRETREATMENT; Energy Analysis; Bioenergy

Citation Formats

Kazi, F K, Fortman, J, Anex, R, Kothandaraman, G, Hsu, D, Aden, A, and Dutta, A. Techno-Economic Analysis of Biochemical Scenarios for Production of Cellulosic Ethanol. United States: N. p., 2010. Web. doi:10.2172/982937.
Kazi, F K, Fortman, J, Anex, R, Kothandaraman, G, Hsu, D, Aden, A, & Dutta, A. Techno-Economic Analysis of Biochemical Scenarios for Production of Cellulosic Ethanol. United States. https://doi.org/10.2172/982937
Kazi, F K, Fortman, J, Anex, R, Kothandaraman, G, Hsu, D, Aden, A, and Dutta, A. 2010. "Techno-Economic Analysis of Biochemical Scenarios for Production of Cellulosic Ethanol". United States. https://doi.org/10.2172/982937. https://www.osti.gov/servlets/purl/982937.
@article{osti_982937,
title = {Techno-Economic Analysis of Biochemical Scenarios for Production of Cellulosic Ethanol},
author = {Kazi, F K and Fortman, J and Anex, R and Kothandaraman, G and Hsu, D and Aden, A and Dutta, A},
abstractNote = {A techno-economic analysis on the production of cellulosic ethanol by fermentation was conducted to understand the viability of liquid biofuel production processes within the next 5-8 years. Initially, 35 technologies were reviewed, then a two-step down selection was performed to choose scenarios to be evaluated in a more detailed economic analysis. The lignocellulosic ethanol process was selected because it is well studied and portions of the process have been tested at pilot scales. Seven process variations were selected and examined in detail. Process designs were constrained to public data published in 2007 or earlier, without projecting for future process improvements. Economic analysis was performed for an 'nth plant' (mature technology) to obtain total investment and product value (PV). Sensitivity analysis was performed on PV to assess the impact of variations in process and economic parameters. Results show that the modeled dilute acid pretreatment process without any downstream process variation had the lowest PV of $3.40/gal of ethanol ($5.15/gallon of gasoline equivalent) in 2007 dollars. Sensitivity analysis shows that PV is most sensitive to feedstock and enzyme costs.},
doi = {10.2172/982937},
url = {https://www.osti.gov/biblio/982937}, journal = {},
number = ,
volume = ,
place = {United States},
year = {Tue Jun 01 00:00:00 EDT 2010},
month = {Tue Jun 01 00:00:00 EDT 2010}
}