ETHANOL-PRODUCTION FROM STARCH IN A PERVAPORATION MEMBRANE BIOREACTOR USING CLOSTRIDIUM-THERMOHYDROSULFURICUM

被引:65
作者
MORI, Y [1 ]
INABA, T [1 ]
机构
[1] MITSUI ENGN & SHIPBLDG CO LTD,CHUOH KU,TOKYO 104,JAPAN
关键词
D O I
10.1002/bit.260360815
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
To attain both high productivity and efficient recovery of ethanol from broth, a membrane bioreactor consisting of a jar fermentor and a pervaporation system was applied to the direct production of ethanol from uncooked starch with a thermophilic anaerobic bacterium, Clostridium thermohydrosulfuricum. From four types of ethanol‐selective membranes tested, microporous polytetrafluoroethylene (PTFE) membrane, the pores of which are impregnated with silicone rubber, was chosen for its large flux, high ethanol selectivity, and high stability. During fed‐batch fermentation with pervaporation in the membrane bioreactor, ethanol was continuously extracted and concentrated in two traps with concentrations at 5.6%–6.2% (w/w) in trap 1 (20 °C) and 27%–32% (w/w) in trap 2 (liquid N2), while the ethanol concentration in the broth was maintained at 0.85–0.9% (w/w). Due to the low ethanol concentration in the broth, and the immobilization of bacterial cells by the membrane, the number of viable cells, and, eventually, the ethanol productivity, increased in the membrane bioreactor. Copyright © 1990 John Wiley & Sons, Inc.
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页码:849 / 853
页数:5
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