National and Local Joint Engineering Research Center for Biomanufacturing of Chiral Chemicals, Zhejiang University of Technology, Hangzhou 310014, People's Republic of China; Key Laboratory of Bioorganic Synthesis of Zhejiang Province, College of Biotechnology and Bioengineering, Zhejiang University of Technology, Hangzhou 310014, People's Republic of China.
National and Local Joint Engineering Research Center for Biomanufacturing of Chiral Chemicals, Zhejiang University of Technology, Hangzhou 310014, People's Republic of China; Key Laboratory of Bioorganic Synthesis of Zhejiang Province, College of Biotechnology and Bioengineering, Zhejiang University of Technology, Hangzhou 310014, People's Republic of China.
Bioresour Technol. 2022 May;352:127024. doi: 10.1016/j.biortech.2022.127024. Epub 2022 Mar 23.
Biosynthesis of D-pantothenate has been widely studied as D-pantothenate is one kind of important vitamins used in food and pharmaceuticals. However, the engineered strain for D-pantothenate production was focused solely on the main biosynthetic pathway, while other important factors such as one carbon unit were ignored. Here the systematic modular engineering on different factors coupled with omics analysis were studied in Escherichia coli for efficient D-pantothenate production. Through reinforcing the precursor pool, refactoring the one carbon unit generation pathway, optimization of reducing power and energy supply, the D-pantothenate titer reached 34.12 g/L with the yield at 0.28 g/g glucose under fed-batch fermentation in 5-L bioreactor. With a further comparative transcriptome and metabolomics studies, the addition of citrate was implemented and 45.35 g/L D-pantothenate was accumulated with a yield of 0.31 g/g glucose. The systematic modular engineering coupled with omics studies provide useful strategies for the industrial production of D-pantothenate.
D-泛酸钙的生物合成已被广泛研究,因为 D-泛酸钙是一种用于食品和药品的重要维生素。然而,用于 D-泛酸钙生产的工程菌株仅专注于主要的生物合成途径,而忽略了其他重要因素,如一碳单位。在这里,通过系统的模块化工程对不同因素进行了研究,并结合组学分析,在大肠杆菌中进行了高效 D-泛酸钙生产。通过增强前体池、重构一碳单位生成途径、优化还原力和能量供应,在 5-L 生物反应器中分批补料发酵下,D-泛酸钙的产量达到 34.12g/L,葡萄糖得率为 0.28g/g。通过进一步的比较转录组学和代谢组学研究,添加了柠檬酸,D-泛酸钙的积累量达到 45.35g/L,葡萄糖得率为 0.31g/g。系统的模块化工程与组学研究相结合,为 D-泛酸钙的工业生产提供了有用的策略。