Yeast fermentation in a cocurrent downflow contacting reactor (CDCR)

被引：0

作者：

Özer, A ^{[1
]}

Dursun, G ^{[1
]}

Özer, D ^{[1
]}

Elibol, M ^{[1
]}

机构：

[1] Firat Univ, Dept Chem Engn, TR-23279 Elazig, Turkey

来源：

JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY | 2000年 / 75卷 / 11期

关键词：

yeast; Monod kinetics; cocurrent downflow contacting reactor; fermentation;

D O I：

10.1002/1097-4660(200011)75:11<1061::AID-JCTB318>3.0.CO;2-K

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：

The growth kinetics and mass transfer characteristics of Saccharomyces cerevisiae in a cocurrent downflow contacting reactor (CDCR) were studied for various glucose concentrations at constant air and liquid flow rates. Increasing glucose concentration increased the biomass concentration thus resulting in an increase in the volumetric oxygen uptake rate. The volumetric mass transfer coefficient, k(L)a, however, decreased with increasing glucose concentration, It was observed that the growth of S cerevisiae in the CDCR would fit the classical Monod kinetics and the maximum specific growth rate was determined to be 0.545 h(-1) (C) 2000 Society of Chemical Industry.

引用

页码：1061 / 1065

页数：5

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