A catalytic multistage fixed-bed tower bioreactor in an industrial-scale pilot plant for alcohol production

被引:0
|
作者
Bakoyianis, V [1 ]
Koutinas, AA [1 ]
机构
[1] UNIV PATRAS,DEPT CHEM,GR-26500 PATRAI,GREECE
关键词
catalytic bioreactor; multistage tower; pilot plant; alcohol; fixed bed;
D O I
10.1002/(SICI)1097-0290(19960120)49:2<197::AID-BIT8>3.0.CO;2-L
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
This article describes the development of an industrial-scale, multistage fixed-bed tower (MFBT) bioreactor using the promoter mineral kissiris for industrial alcohol production using free cells. Specifically, we examined the parameters needed to maintain operational stability from batch to batch for long periods. Pilot plant operations used one- and two-stage fixed-bed, 7000-L bioreactors. Likewise a 100,000-L, multistage fixed-bed tower system containing layered kissiris confirmed the laboratory results. Compared with a continuous stirred tank fermenter (CSTF) with recycle, a 30% reduction of energy demand and 10%-20% of the production costs are obtained. The latter are attributed to the increased ethanol concentration and alcohol productivity. (C) 1996 John Wiley & Sons, Inc.
引用
收藏
页码:197 / 203
页数:7
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