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用于高效生产乙醇酸的大肠杆菌代谢工程的多种策略。

Multiple strategies for metabolic engineering of Escherichia coli for efficient production of glycolate.

作者信息

Zhu Tong, Yao Die, Li Di, Xu Hongtao, Jia Shiru, Bi Changhao, Cai Jun, Zhu Xinna, Zhang Xueli

机构信息

College of Biotechnology, Tianjin University of Science and Technology, Tianjin, China.

Tianjin Institute of Industrial Biotechnology, Chinese of Academy of Sciences, Tianjin, China.

出版信息

Biotechnol Bioeng. 2021 Dec;118(12):4699-4707. doi: 10.1002/bit.27934. Epub 2021 Sep 15.

Abstract

Glycolate is a bulk chemical with wide applications in the textile, food processing, and pharmaceutical industries. Glycolate can be produced from glucose via the glycolysis and glyoxylate shunt pathways, followed by reduction to glycolate. However, two problems limit the productivity and yield of glycolate when using glucose as the sole carbon source. The first is a cofactor imbalance in the production of glycolate from glucose via the glycolysis pathway, since NADPH is required for glycolate production, while glycolysis generates NADH. To rectify this imbalance, the NADP -dependent glyceraldehyde 3-phosphate dehydrogenase GapC from Clostridium acetobutylicum was introduced to generate NADPH instead of NADH in the oxidation of glyceraldehyde 3-phosphate during glycolysis. The soluble transhydrogenase SthA was further eliminated to conserve NADPH by blocking its conversion into NADH. The second problem is an unfavorable carbon flux distribution between the tricarboxylic acid cycle and the glyoxylate shunt. To solve this problem, isocitrate dehydrogenase (ICDH) was eliminated to increase the carbon flux of glyoxylate and thereby improve the glycolate titer. After engineering through the integration of gapC, combined with the inactivation of ICDH, SthA, and by-product pathways, as well as the upregulation of the two key enzymes isocitrate lyase (encoding by aceA), and glyoxylate reductase (encoding by ycdW), the glycolate titer increased to 5.3 g/L with a yield of 1.89 mol/mol glucose. Moreover, an optimized fed-batch fermentation reached a titer of 41 g/L with a yield of 1.87 mol/mol glucose after 60 h.

摘要

乙醇酸是一种大宗化学品,在纺织、食品加工和制药行业有广泛应用。乙醇酸可通过糖酵解和乙醛酸分流途径由葡萄糖生产,随后还原为乙醇酸。然而,当使用葡萄糖作为唯一碳源时,有两个问题限制了乙醇酸的生产率和产量。第一个问题是通过糖酵解途径由葡萄糖生产乙醇酸时的辅因子失衡,因为乙醇酸生产需要NADPH,而糖酵解产生NADH。为纠正这种失衡,引入了来自丙酮丁醇梭菌的依赖NADP的3-磷酸甘油醛脱氢酶GapC,以便在糖酵解过程中3-磷酸甘油醛氧化时生成NADPH而非NADH。进一步去除了可溶性转氢酶SthA,通过阻止其转化为NADH来保存NADPH。第二个问题是三羧酸循环和乙醛酸分流之间不利的碳通量分布。为解决这个问题,去除了异柠檬酸脱氢酶(ICDH)以增加乙醛酸的碳通量,从而提高乙醇酸滴度。通过整合gapC进行工程改造,结合ICDH、SthA和副产物途径的失活,以及两个关键酶异柠檬酸裂解酶(由aceA编码)和乙醛酸还原酶(由ycdW编码)的上调,乙醇酸滴度提高到5.3 g/L,产率为1.89 mol/mol葡萄糖。此外,优化的补料分批发酵在60小时后达到了41 g/L的滴度,产率为1.87 mol/mol葡萄糖。

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