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A modular metabolic engineering approach for the production of 1,2-propanediol from glycerol by Saccharomyces cerevisiae

机译:一种模块化的代谢工程方法,用于由酿酒酵母(saccharomyces cerevisiae)从甘油生产1,2-丙二醇

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摘要

Compared to sugars, a major advantage of using glycerol as a feedstock for industrial bioprocesses is the fact that this molecule is more reduced than sugars. A compound whose biotechnological production might greatly profit from the substrate's higher reducing power is 1,2-propanediol (1,2-PDO). Here we present a novel metabolic engineering approach to produce 1,2-PDO from glycerol in S. cerevisiae. Apart from implementing the heterologous methylglyoxal (MG) pathway for 1,2-PDO formation from dihydroxyacetone phosphate (DHAP) and expressing a heterologous glycerol facilitator, the employed genetic modifications included the replacement of the native FAD-dependent glycerol catabolic pathway by the `DHA pathway´ for delivery of cytosolic NADH and the reduction of triosephosphate isomerase (TPI) activity for increased precursor (DHAP) supply. The choice of the medium had a crucial impact on both the strength of the metabolic switch towards fermentation in general (as indicated by the production of ethanol and 1,2-PDO) and on the ratio at which these two fermentation products were formed. For example, virtually no 1,2-PDO but only ethanol was formed in synthetic glycerol medium with urea as the nitrogen source. When nutrient-limited complex YG medium was used, significant amounts of 1,2-PDO were formed and it became obvious that the concerted supply of NADH and DHAP are essential for boosting 1,2-PDO production. Additionally, optimizing the flux into the MG pathway improved 1,2-PDO formation at the expense of ethanol. Cultivation of the best-performing strain in YG medium and a controlled bioreactor set-up resulted in a maximum titer of 4gL-1 1,2-PDO which, to the best of our knowledge, has been the highest titer of 1,2-PDO obtained in yeast so far. Surprisingly, significant 1,2-PDO production was also obtained in synthetic glycerol medium after changing the nitrogen source towards ammonium sulfate and adding a buffer.
机译:与糖相比,使用甘油作为工业生物处理的原料的主要优点是该分子比糖更加减少。一种化合物,其生物技术生产可能从基质的较高的降低功率下利润是1,2-丙二醇(1,2-PDO)。在这里,我们提出了一种新的代谢工程方法,从酿酒酵母中产生1,2-PDO。除了从二羟基丙酮磷酸酯(DHAP)中的1,2-PDO形成的异源甲基甘油(Mg)途径外,所用的遗传修饰包括替代`DHA的天然依赖于依赖甘油分解代谢途径的替代遗传修饰用于递送细胞溶质NADH的途径和用于增加前体(DHAP)供应的Triosephosphate异构酶(TPI)活性的减少。介质的选择通常对代谢切换的强度朝向发酵的强度(如乙醇和1,2-PDO的生产所示),并且在形成这两个发酵产物的比例上。例如,几乎没有1,2-PDO,但仅在具有尿素的合成甘油培养基中形成乙醇作为氮源。当使用营养有限的复合YG培养基时,形成大量的1,2-PDO,并且显而易见的是,NADH和DHAP的协调供应对于提高1,2-PDO生产是必不可少的。另外,以乙醇为代价优化进入Mg途径的通量改善1,2-PDO形成。培养yg培养基和受控生物反应器设置中最佳性能的培养导致最大滴度> 4gl-1 1,2-pdo,这是我们最知识的最高滴度为1,2 - 到目前为止,在酵母中获得的pdo。令人惊讶的是,在将氮源朝向硫酸铵和添加缓冲液中,在合成甘油培养基中也可以在合成甘油培养基中获得显着的1,2-PDO产生。

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