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Microbial production of 1,3-propanediol in Escherichia coli: A model system for metabolic engineering.

机译:大肠杆菌中1,3-丙二醇的微生物生产:用于代谢工程的模型系统。

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Metabolic engineering involves the use of recombinant DNA technology to construct or modify metabolic pathways in cells. The production of 1,3-propanediol (1,3-PD) in E. coli was chosen as a model system for metabolic engineering. The source of the 1,3-PD pathway genes was K. pneumoniae ATCC 25955. An enrichment for anaerobic glycerol and dihydroxyacetone (DHA) utilization, followed by screening for 1,3-PD producers resulted in the identification of E. coli AG1/pTC1 from a genomic library of K. pneumoniae. At least four genes of the dha regulon were transferred into pTC1. The yield of 1,3-PD from glycerol was 0.46 mol/mol.; Directions for further improvements of 1,3-PD production in E. coli were explored based on the stoichiometric/topological constraints and kinetic constraints. Several ideas from the above analyses were then implemented to complete the cycle between theoretical prediction and experimentation.; Cofermentation of glycerol and sugars was used as a physiological approach to overcome the topological/stoichiometric constraints. The yield of 1,3-PD by E. coli AG1/pTC1 was 0.63 mol/mol in a cofermentation of glycerol and glucose. Genetic manipulation was used to overcome the kinetic constraints. The genes of the dha regulon in cosmid pTC1 were subcloned into pBR322, and were also transferred into pBluescript II SK(+). The DHA kinase activity from the gene dhaK was further inactivated by an insertional mutation.; Cofermentations of glycerol and glucose by E. coli with new versions of pTC plasmids in 300 ml anaerobic flasks showed significant improvements in the yield of 1,3-PD from glycerol. A 5-l fed-batch cofermentation of glycerol and glucose by E. coli AG1/pTC9 gave yields of 1,3-PD ranging from 0.85 to 0.97 with different glucose to glycerol ratios. The highest productivity, 0.54 g/l/h, was observed with a glucose to glycerol ratio of 1.0 g/g. The final 1,3-PD concentration was 6.72 g/l with an overall productivity of 0.24 g/l/h by E. coli AG1/pTC9. The study of 1,3-PD production in E. coli demonstrates that metabolic engineering is a very powerful approach for process development in biotechnology.
机译:代谢工程涉及使用重组DNA技术来构建或修饰细胞中的代谢途径。选择在大肠杆菌中生产1,3-丙二醇(1,3-PD)作为代谢工程的模型系统。 1,3-PD途径基因的来源是肺炎克雷伯菌ATCC25955。对厌氧甘油和二羟基丙酮(DHA)的利用进行了富集,然后筛选了1,3-PD生产者,从而鉴定了大肠杆菌AG1 /来自肺炎克雷伯菌基因组文库的pTC1。 dha regulon的至少四个基因被转移到pTC1中。由甘油得到的1,3-PD为0.46mol / mol。基于化学计量/拓扑约束和动力学约束,探索了进一步改善大肠杆菌1,3-PD生产的方向。然后,从上述分析中得到了一些想法,以完成理论预测和实验之间的循环。甘油和糖的共同发酵被用作克服拓扑/化学计量约束的生理方法。在甘油和葡萄糖的共同发酵中,大肠杆菌AG1 / pTC1的1,3-PD的产率为0.63mol / mol。遗传操纵被用来克服动力学约束。粘粒pTC1中的dha regulon基因被亚克隆到pBR322中,也被转移到pBluescript II SK(+)中。来自dhaK基因的DHA激酶活性被插入突变进一步失活。大肠杆菌与新版本的pTC质粒在300 ml厌氧烧瓶中对甘油和葡萄糖的发酵表明,甘油的1,3-PD收率得到了显着提高。大肠杆菌AG1 / pTC9对甘油和葡萄糖的5:1补料分批发酵,在不同的葡萄糖和甘油比率下,1,3-PD的产量为0.85-0.97。葡萄糖与甘油之比为1.0 g / g时,观察到最高的生产率0.54 g / l / h。大肠杆菌AG1 / pTC9的最终1,3-PD浓度为6.72 g / l,总生产率为0.24 g / l / h。对大肠杆菌中1,3-PD生产的研究表明,代谢工程是生物技术过程开发中非常有效的方法。

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