Continuous high-solids corn liquefaction and fermentation with stripping of ethanol.
Removal of ethanol from the fermentor during fermentation can increase productivity and reduce the costs for dewatering the product and coproduct. One approach is to recycle the fermentor contents through a stripping column, where a non-condensable gas removes ethanol to a condenser. Previous research showed that this approach is feasible. Savings of $0.03 per gallon were predicted at 34% corn dry solids. Greater savings were predicted at higher concentration. Now the feasibility has been demonstrated at over 40% corn dry solids, using a continuous corn liquefaction system. A pilot plant, that continuously fed corn meal at more than one bushel (25 kg) per day, was operated for 60 consecutive days, continuously converting 95% of starch and producing 88% of the maximum theoretical yield of ethanol. A computer simulation was used to analyze the results. The fermentation and stripping systems were not significantly affected when the CO(2) stripping gas was partially replaced by nitrogen or air, potentially lowering costs associated with the gas recycle loop. It was concluded that previous estimates of potential cost savings are still valid.
U.S. Department of Agriculture, Agricultural Research Service, Eastern Regional Research Center, 600 E. Mermaid Lane, Wyndmoor, PA 19038, USA. frank.taylor@ars.usda.gov
Frank
F
Taylor
Marco A
MA
Marquez
David B
DB
Johnston
Neil M
NM
Goldberg
Kevin B
KB
Hicks
D001709:Biotechnology / Q000379:methods*; D002851:Chromatography, High Pressure Liquid; D003198:Computer Simulation; D000431:Ethanol / Q000302:isolation & purification*; D005285:Fermentation / Q000187:drug effects; D005947:Glucose / Q000494:pharmacology; D007700:Kinetics; D013696:Temperature; D013997:Time Factors; D003313:Zea mays / Q000187:drug effects / Q000378:metabolism*
D000431:Ethanol; D005947:Glucose