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在厌氧条件下,通过大肠杆菌的代谢工程从大豆水解物中生产琥珀酸。

Metabolic engineering of Escherichia coli to produce succinate from soybean hydrolysate under anaerobic conditions.

机构信息

Department of BioSciences, Rice University, Houston, Texas.

Institute of Bioengineering, Zhejiang University of Technology, Hangzhou, P. R. China.

出版信息

Biotechnol Bioeng. 2018 Jul;115(7):1743-1754. doi: 10.1002/bit.26584. Epub 2018 Mar 24.

DOI:10.1002/bit.26584
PMID:29508908
Abstract

It is of great economic interest to produce succinate from low-grade carbon sources, which can enhance the competitiveness of the biological route. In this study, succinate producer Escherichia coli CT550/pHL413KF1 was further engineered to efficiently use the mixed sugars from non-food based soybean hydrolysate to produce succinate under anaerobic conditions. Since many common E. coli strains fail to use galactose anaerobically even if they can use it aerobically, the glucose, and galactose related sugar transporters were deactivated individually and evaluated. The PTS system was found to be important for utilization of mixed sugars, and galactose uptake was activated by deactivating ptsG. In the ptsG strain, glucose, and galactose were used simultaneously. Glucose was assimilated mainly through the mannose PTS system while galactose was transferred mainly through GalP in a ptsG strain. A new succinate producing strain, FZ591C which can efficiently produce succinate from the mixed sugars present in soybean hydrolysate was constructed by integration of the high succinate yield producing module and the galactose utilization module into the chromosome of the CT550 ptsG strain. The succinate yield reached 1.64 mol/mol hexose consumed (95% of maximum theoretical yield) when a mixed sugars feedstock was used as a carbon source. Based on the three monitored sugars, a nominal succinate yield of 1.95 mol/mol was observed as the strain can apparently also use some other minor sugars in the hydrolysate. In this study, we demonstrate that FZ591C can use soybean hydrolysate as an inexpensive carbon source for high yield succinate production under anaerobic conditions, giving it the potential for industrial application.

摘要

从低品位碳源生产琥珀酸具有重要的经济意义,可以提高生物途径的竞争力。在这项研究中,进一步工程改造琥珀酸生产菌大肠杆菌 CT550/pHL413KF1,使其能够在厌氧条件下有效地利用非食用大豆水解物中的混合糖生产琥珀酸。由于许多常见的大肠杆菌菌株即使能够在有氧条件下使用半乳糖,也无法在厌氧条件下使用,因此单独失活并评估了葡萄糖和半乳糖相关的糖转运蛋白。发现 PTS 系统对半乳糖的利用很重要,失活 ptsG 可激活半乳糖摄取。在 ptsG 菌株中,葡萄糖和半乳糖同时被利用。葡萄糖主要通过 mannose PTS 系统同化,而半乳糖主要通过 ptsG 菌株中的 GalP 转移。通过将高产琥珀酸的生产模块和半乳糖利用模块整合到 CT550 ptsG 菌株的染色体中,构建了能够从大豆水解物中的混合糖高效生产琥珀酸的新生产菌株 FZ591C。当使用混合糖作为碳源时,琥珀酸的产率达到 1.64 mol/mol 己糖消耗(95%最大理论产率)。基于三种监测糖,观察到名义琥珀酸产率为 1.95 mol/mol,因为该菌株显然也可以利用水解物中的一些其他少量糖。在这项研究中,我们证明了 FZ591C 可以使用大豆水解物作为厌氧条件下高产琥珀酸生产的廉价碳源,因此具有工业应用的潜力。

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