期刊
ENZYME AND MICROBIAL TECHNOLOGY
卷 28, 期 2-3, 页码 189-195出版社
ELSEVIER SCIENCE INC
DOI: 10.1016/S0141-0229(00)00288-X
关键词
batch fermentation; Yarrowia lipolytica; citric acid; biomass-recycle fermentor
This experimental study reports about production selectivity in the fermentation of glucose to citric acid by Yarrowia lipolytica as a function of substrate concentration. Batch runs featuring biomass growth and one or two citric acid production phases were carried out in a 15-1 stirred tank fermenter. The presented results demonstrate that working at high initial substrate concentration in the production phase is beneficial both in terms of a higher production rate of citric acid, the desired metabolite (reaching 0.077 h(-1)) and of a higher utilization degree of the employed carbon source (yield up to 0.384 g(c.a)/g(glucose)). The production rate of isocitric acid, the major undesired metabolite, was found to be practically constant over the tested initial substrate concentration range. (C) 2001 Elsevier Science Inc. All rights reserved.
作者
我是这篇论文的作者
点击您的名字以认领此论文并将其添加到您的个人资料中。
推荐
暂无数据