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Enhanced production of (R)-1,8-propanediol by metabolically engineeredEscherichia coli

机译:通过代谢工程改造的大肠杆菌提高(R)-1,8-丙二醇的产量

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1,2-Propanediol (1,2-PD) is a major commodity chemical currently derived from propylene. Previously, we have demonstrated the production of enantiomerically pure (R)-1,2-propanediol from glucose by an engineered E. coli expressing genes for NADH-linked glycerol dehydrogenase and methylglyoxal synthase. In this work, we investigate three methods to improve 1,2-PD in E. coli. First, we investigated improving the host by eliminating production of a byproduct, lactate. To do this, we constructed strains with mutations in two enzymes involved in lactate production, lactate dehydrogenase and glyoxalase I. (Surprisingly, when mutations were made in its ability to produce lactate, one strain of E. coli [MM294], produced a small amount of 1,2-PD without any added genes.) Second, we constructed a complete pathway to 1,2-PD from the glycolytic intermediate, dihydroxyacetone phosphate. Our previous 1,2-PD producing strains relied on at least one endogenous E. coli activity and only produced 0.7 g/L of 1,2-PD. The complete pathway involved the coexpression of methylglyoxal synthase (mgs), glycerol dehydrogenase (gldA), and either yeast alcohol dehydrogenase (adhI) or E. coli 1,2-propanediol oxidoreductase (fucO). Third, we investigated bioprocessing improvements by carrying out a fed-batch fermentation with the best engineered strain (expressing mgs, gldA, and fucO). A final titer of 4.5 g/L of(R)-1,S-PD was produced, with a final yield of 0.19 g of 1,2-PD per gram of glucose consumed. This work provides a basis for further strain and process improvement.
机译:1,2-丙二醇(1,2-PD)是目前衍生自丙烯的主要商品化学品。以前,我们已经证明了通过工程改造的表达NADH连接的甘油脱氢酶和甲基乙二醛合酶基因的大肠杆菌从葡萄糖生产对映体纯的(R)-1,2-丙二醇。在这项工作中,我们研究了三种改善大肠杆菌中1,2-PD的方法。首先,我们研究了通过消除副产物乳酸的产生来改善宿主的方法。为此,我们构建了在乳酸生产中涉及的两种酶(乳酸脱氢酶和乙二醛酶I)中具有突变的菌株。(令人惊讶的是,当产生乳酸的能力发生突变时,一株大肠杆菌[MM294]产生了少量量的1,2-PD,而无需添加任何基因。)其次,我们从糖酵解中间体磷酸二羟基丙酮构建了一条通往1,2-PD的完整途径。我们之前生产1,2-PD的菌株至少依赖一种内源性大肠杆菌活性,仅产生0.7 g / L的1,2-PD。完整途径涉及甲基乙二醛合酶(mgs),甘油脱氢酶(gldA)和酵母醇脱氢酶(adhI)或大肠杆菌1,2-丙二醇氧化还原酶(fucO)的共表达。第三,我们通过用最佳工程菌株(表达mgs,gldA和fucO)进行分批补料发酵研究了生物工艺的改进。最终滴度为4.5 g / L -1,S-PD,每克消耗的葡萄糖最终产量为0.19 g 1,2-PD。这项工作为进一步的应变和工艺改进提供了基础。

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