CONTINUOUS PRODUCTION OF HIGH ETHANOL SOLUTION USING AN IMMOBILIZED YEAST BIOREACTOR
被引:0
作者:
SUEKI, M
论文数: 0引用数: 0
h-index: 0
机构:
KIRIN BREWERY,TSURUMI KU,YOKOHAMA 230,JAPANKIRIN BREWERY,TSURUMI KU,YOKOHAMA 230,JAPAN
SUEKI, M
[1
]
ARIKAWA, K
论文数: 0引用数: 0
h-index: 0
机构:
KIRIN BREWERY,TSURUMI KU,YOKOHAMA 230,JAPANKIRIN BREWERY,TSURUMI KU,YOKOHAMA 230,JAPAN
ARIKAWA, K
[1
]
SUZUKI, A
论文数: 0引用数: 0
h-index: 0
机构:
KIRIN BREWERY,TSURUMI KU,YOKOHAMA 230,JAPANKIRIN BREWERY,TSURUMI KU,YOKOHAMA 230,JAPAN
SUZUKI, A
[1
]
机构:
[1] KIRIN BREWERY,TSURUMI KU,YOKOHAMA 230,JAPAN
来源:
HAKKOKOGAKU KAISHI-JOURNAL OF THE SOCIETY OF FERMENTATION TECHNOLOGY
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1991年
/
69卷
/
01期
关键词:
D O I:
暂无
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:
A newly-developed cascade feed technique using two reactors was applied to the continuous production of a high ethanol solution. Ethanol solution more than 15 vol% was continuously produced for about 50 days. Simulations of the cascade feed technique with the two reactors were carried out, using mathematical equations which approximated the actual approximated the actual distribution of glucose and ethanol in an immobilized yeast bioreactor. The simulated results showed that the first reactor should be operated so as to assimilate most of the charged glucose.