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调整主要生物合成模块以提高大肠杆菌W3110中L-高丝氨酸的产量。

Adjustment of the main biosynthesis modules to enhance the production of l-homoserine in Escherichia coli W3110.

作者信息

Niu Kun, Zheng Rui, Zhang Miao, Chen Mao-Qin, Kong Yi-Ming, Liu Zhi-Qiang, Zheng Yu-Guo

机构信息

The National and Local Joint Engineering Research Center for Biomanufacturing of Chiral Chemicals, Zhejiang University of Technology, Hangzhou, China.

Key Laboratory of Bioorganic Synthesis of Zhejiang Province, College of Biotechnology and Bioengineering, Zhejiang University of Technology, Hangzhou, China.

出版信息

Biotechnol Bioeng. 2025 Jan;122(1):223-232. doi: 10.1002/bit.28861. Epub 2024 Oct 18.

Abstract

l-homoserine is an important platform compound of many valuable products. Construction of microbial cell factory for l-homoserine production from glucose has attracted a great deal of attention. In this study, l-homoserine biosynthesis pathway was divided into three modules, the glucose uptake and upstream pathway, the downstream pathway, and the energy supply module. Metabolomics of the chassis strain HS indicated that the supply of ATP was inadequate, therefore, the energy supply module was firstly modified. By balancing the ATP supply module, the l-homoserine production increased by 66% to 12.55 g/L. Further, the results indicated that the upstream pathway was blocked, and increasing the culture temperature to 37°C could solve this problem and the l-homoserine production reached 21.38 g/L. Then, the downstream synthesis pathways were further strengthened to balance the fluxes, and the l-homoserine production reached the highest reported level of 32.55 g/L in shake flasks. Finally, fed-batch fermentation in a 5-L bioreactor was conducted, and l-homoserine production could reach to 119.96 g/L after 92 h cultivation, with the yield of 0.41 g/g glucose and productivity of 1.31 g/L/h. The study provides a well research foundation for l-homoserine production by microbial fermentation with the capacity for industrial application.

摘要

L-高丝氨酸是许多有价值产品的重要平台化合物。构建以葡萄糖为原料生产L-高丝氨酸的微生物细胞工厂已引起广泛关注。在本研究中,L-高丝氨酸生物合成途径被分为三个模块,即葡萄糖摄取及上游途径、下游途径和能量供应模块。底盘菌株HS的代谢组学分析表明ATP供应不足,因此首先对能量供应模块进行了改造。通过平衡ATP供应模块,L-高丝氨酸产量提高了66%,达到12.55 g/L。进一步研究结果表明上游途径受阻,将培养温度提高到37°C可解决此问题,L-高丝氨酸产量达到21.38 g/L。然后,进一步强化下游合成途径以平衡通量,L-高丝氨酸产量在摇瓶中达到了报道的最高水平32.55 g/L。最后,在5-L生物反应器中进行补料分批发酵,培养92 h后L-高丝氨酸产量可达119.96 g/L,葡萄糖产率为0.41 g/g,生产速率为1.31 g/L/h。该研究为微生物发酵生产L-高丝氨酸提供了良好的研究基础,具有工业应用潜力。

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