Two‐stage carbon distribution and cofactor generation for improving l‐threonine production of Escherichia coli

生物化学 苏氨酸 柠檬酸循环 辅因子 磷酸烯醇丙酮酸羧激酶 化学 大肠杆菌 生物 丝氨酸 新陈代谢 基因
作者
Jiaheng Liu,Huiling Li,Hui Xiong,Xixian Xie,Ning Chen,Guang-Rong Zhao,Qinggele Caiyin,Hongji Zhu,Jianjun Qiao
出处
期刊:Biotechnology and Bioengineering [Wiley]
卷期号:116 (1): 110-120 被引量:39
标识
DOI:10.1002/bit.26844
摘要

L-Threonine, a kind of essential amino acid, has numerous applications in food, pharmaceutical, and aquaculture industries. Fermentative l-threonine production from glucose has been achieved in Escherichia coli. However, there are still several limiting factors hindering further improvement of l-threonine productivity, such as the conflict between cell growth and production, byproduct accumulation, and insufficient availability of cofactors (adenosine triphosphate, NADH, and NADPH). Here, a metabolic modification strategy of two-stage carbon distribution and cofactor generation was proposed to address the above challenges in E. coli THRD, an l-threonine producing strain. The glycolytic fluxes towards tricarboxylic acid cycle were increased in growth stage through heterologous expression of pyruvate carboxylase, phosphoenolpyruvate carboxykinase, and citrate synthase, leading to improved glucose utilization and growth performance. In the production stage, the carbon flux was redirected into l-threonine synthetic pathway via a synthetic genetic circuit. Meanwhile, to sustain the transaminase reaction for l-threonine production, we developed an l-glutamate and NADPH generation system through overexpression of glutamate dehydrogenase, formate dehydrogenase, and pyridine nucleotide transhydrogenase. This strategy not only exhibited 2.02- and 1.21-fold increase in l-threonine production in shake flask and bioreactor fermentation, respectively, but had potential to be applied in the production of many other desired oxaloacetate derivatives, especially those involving cofactor reactions.
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