Process Design and Economics for Biochemical Conversion of Lignocellulosic Biomass to Ethanol: Dilute-Acid Pretreatment and Enzymatic Hydrolysis of Corn Stover

Проектирование процесса и экономика биохимической конверсии лигноцеллюлозной биомассы в этанол: разбавленная кислотная предобработка и ферментативный гидролиз кукурузных стеблей и листьев
David Humbird, Ryan Davis, Ling Tao, Christopher Kinchin, David Hsu, A. Aden, P. Schoen, John C. Lukas, B Olthof, M. Worley, Danielle Sexton, D Dudgeon
2011-03-01

Biochemical ethanol conversionCorn stoverDilute-acid pretreatmentEnzymatic saccharificationProcess economics
This report describes one potential biochemical ethanol conversion process, conceptually based upon core conversion and process integration research at NREL. The overarching process design converts corn stover to ethanol by dilute-acid pretreatment, enzymatic saccharification, and co-fermentation. Building on design reports published in 2002 and 1999, NREL, together with the subcontractor HarrisGroup Inc., performed a complete review of the process design and economic model for the biomass-to-ethanol process. This update reflects NREL's current vision of the biochemical ethanol process and includes the latest research in the conversion areas (pretreatment, conditioning, saccharification, and fermentation), optimizations in product recovery, and our latest understanding of the ethanolplant's back end (wastewater and utilities). The conceptual design presented here reports ethanol production economics as determined by 2012 conversion targets and 'nth-plant' project costs and financing. For the biorefinery described here, processing 2,205 dry ton/day at 76% theoretical ethanol yield (79 gal/dry ton), the ethanol selling price is $2.15/gal in 2007$.
1
At a processing capacity of 2,205 dry tons per day and 76% theoretical ethanol yield, equivalent to 79 gallons per dry ton, the projected ethanol selling price is $2.15 per gallon in 2007 dollars.
2
NREL and HarrisGroup comprehensively updated the process design and economic model, incorporating advances in pretreatment, conditioning, saccharification, fermentation, product recovery, wastewater, and utilities.
3
The conceptual biorefinery converts corn stover to ethanol through dilute-acid pretreatment, enzymatic saccharification, and co-fermentation.
4
The design reflects 2012 conversion targets and nth-plant project costs and financing assumptions.

Corn stover biochemical ethanol conversion process

Process design and economic performance, including conversion efficiency and ethanol selling price, under dilute-acid pretreatment, enzymatic saccharification, co-fermentation, and integrated biorefinery operations

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2011-03-01
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David Humbird
Ryan Davis
Ling Tao
Christopher Kinchin
David Hsu
A. Aden
P. Schoen
John C. Lukas
B Olthof
M. Worley
Danielle Sexton
D Dudgeon
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