Enhanced α-ketoglutaric acid production in Yarrowia lipolytica WSH-Z06 by an improved integrated fed-batch strategy

被引:55
|
作者
Yu, Zongzhong [1 ]
Du, Guocheng [2 ,3 ]
Zhou, Jingwen [1 ,2 ]
Chen, Jian [1 ,2 ]
机构
[1] Jiangnan Univ, Sch Biotechnol, State Key Lab Food Sci & Technol, 1800 Lihu Rd, Wuxi 214122, Jiangsu, Peoples R China
[2] Jiangnan Univ, Minist Educ, Key Lab Carbohydrate Chem & Biotechnol, Wuxi 214122, Jiangsu, Peoples R China
[3] Jiangnan Univ, Minist Educ, Key Lab Ind Biotechnol, Wuxi 214122, Jiangsu, Peoples R China
基金
中国国家自然科学基金;
关键词
alpha-Ketoglutaric acid; pH control strategy; Fed-batch; Yarrowia lipolytica; Overproduction; TORULOPSIS-GLABRATA; CARBON FLUX; CALCIUM LEVEL; YEAST; PYRUVATE; REDISTRIBUTION; OVERPRODUCTION; OPTIMIZATION; PERFORMANCE; SECRETION;
D O I
10.1016/j.biortech.2012.03.021
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
This study aimed at enhancing alpha-ketoglutaric acid (alpha-KG) production by Yarrowia lipolytica WSH-206. Batch culture experiments demonstrated that CaCO3 and a relatively low pH (3.0) in the alpha-KG production phase contributed to alpha-KG synthesis. Using a two-stage pH control strategy, in which pH was buffered by CaCO3 in the growth phase and then maintained at 3.0 in the alpha-KG production phase, the yield of alpha-KG reached 53.4 g L-1. In the later phase of batch fermentation, the glycerol was exhausted but synthesis of alpha-KG did not cease. Therefore, glycerol was fed with an integrated fed-batch mode, and alpha-KG production increased to 66.2 g L-1 with a productivity of 0.35 g L-1 h(-1). Compared to optimal batch culture, alpha-KG production and productivity were enhanced by 23.9% and 16.7%, respectively. The two-stage pH control strategy, constant feeding approach and lower pH in later phase would be useful for alpha-KG industrial production. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:597 / 602
页数:6
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