RAPID ETHANOL FERMENTATION OF CELLULOSE HYDROLYSATE .1. BATCH VERSUS CONTINUOUS SYSTEMS

被引:191
作者
GHOSE, TK
TYAGI, RD
机构
[1] Biochemical Engineering Research Centre, Indian Institute of Technology, New Delhi, 110029, Delhi, Hauz Khas
关键词
D O I
10.1002/bit.260210807
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
Rapid fermentation of bagasse hydrolysate to ethanol under anaerobic conditions by a strain of Saccharomyces cerevisiae has been studied in batch and continuous cultures at pH 4.0 and 30°C temperature with cell recycle. By using a 23.6 g/liter cell concentration, a concentation of 9.7% (w/v)ethanol was developed in a period of 6 hr. The rate of fermentation was found to increase with supplementation of yeast vitamins in the hydrolysate. In continuous culture employing cell recycle and a 0.127 v/v/m air flow rate, a cell mass concentration of 48.5 g/liter has been achieved. The maximum fermentor productivity of ethanol obtained under these conditions was 32.0 g/liter/hr, which is nearly 7.5 times higher than the normal continuous process without cell recycle and air sparging. The ethanol productivity was found to decrease linearly with ethanol concentration. Conversion of glucose in the hydrolysate to ethanol was achieved with a yield of 95 to 97% of theoretical. Copyright © 1979 John Wiley & Sons, Inc.
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页码:1387 / 1400
页数:14
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