详细信息

Development of a High-Titer Culture Medium for the Production of Cholesterol by Engineered Saccharomyces cerevisiae and Its Fed-Batch Cultivation Strategy  ( SCI-EXPANDED收录)  

文献类型:期刊文献

英文题名:Development of a High-Titer Culture Medium for the Production of Cholesterol by Engineered Saccharomyces cerevisiae and Its Fed-Batch Cultivation Strategy

作者:Wang, Ling-Xu[1];Zheng, Gao-Fan[1];Xin, Xiu-Juan[1];An, Fa-Liang[1]

机构:[1]East China Univ Sci & Technol, State Key Lab Bioreactor Engn, Shanghai 200237, Peoples R China

年份:2022

卷号:32

期号:9

起止页码:1178

外文期刊名:JOURNAL OF MICROBIOLOGY AND BIOTECHNOLOGY

收录:;WOS:【SCI-EXPANDED(收录号:WOS:000864871700012)】;

语种:英文

外文关键词:Cholesterol; S; cerevisiae; fermentation optimization; fed -batch culture; citric acid

摘要:Steroids are a class of compounds with cyclopentane polyhydrophenanthrene as the parent nucleus, and they usually have unique biological and pharmacological activities. Most of the biosynthesis of steroids is completed by a series of enzymatic reactions starting from cholesterol. Synthetic biology can be used to synthesize cholesterol in engineered microorganisms, but the production of cholesterol is too low to further produce other high-value steroids from cholesterol as the raw material and precursor. In this work, combinational strategies were established to increase the production of cholesterol in engineered Saccharomyces cerevisiae RH6829. The basic medium for high cholesterol production was selected by screening 8 kinds of culture media. Single-factor optimization of the carbon and nitrogen sources of the culture medium, and the addition of calcium ions, zinc ions and citric acid, further increased the cholesterol production to 192.53 mg/l. In the 5-L bioreactor, through the establishment of strategies for glucose and citric acid feeding and dissolved oxygen regulation, the cholesterol production was further increased to 339.87 mg/l, which was 734% higher than that in the original medium. This is the highest titer of cholesterol produced by microorganisms currently reported. The fermentation program has also been conducted in a 50-L bioreactor to prove its stability and feasibility.

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