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Metabolic engineering of Escherichia coli to minimize byproduct formate and improving succinate productivity through increasing NADH availability by heterologous expression of NAD+-dependent formate dehydrogenase

格式化 甲酸脱氢酶 混合酸发酵 代谢工程 发酵 生物化学 琥珀酸 化学 NAD+激酶 生物 细菌 催化作用 乳酸 乳酸发酵 遗传学
作者
Grant J. Balzer,Chandresh Thakker,George N. Bennett,Ka‐Yiu San
出处
期刊:Metabolic Engineering [Elsevier BV]
卷期号:20: 1-8 被引量:104
标识
DOI:10.1016/j.ymben.2013.07.005
摘要

Succinic acid is a specialty chemical having numerous applications in industrial, pharmaceutical and food uses. One of the major challenges in the succinate fermentation process is eliminating the formation of byproducts. In this study, we describe eliminating byproduct formate and improving succinate productivity by reengineering a high succinate producing E. coli strain SBS550MG-Cms243(pHL413Km). The NAD+-dependent formate dehydrogenase gene (fdh1) of Candida boidinii was coexpressed with Lactococcus lactis pyruvate carboxylase (pycA) under the control of Ptrc and PpycA promoters in plasmid pHL413KF1. The newly introduced fdh1 converts 1 mol of formate into 1 mol of NADH and CO2. The reengineered strain SBS550MG-Cms243(pHL413KF1) retains the reducing power of formate through an increase in NADH availability. In anaerobic shake flask fermentations, the parent strain SBS550MG-Cms243(pHL413Km) consumed 99.86 mM glucose and produced 172.38 mM succinate, 16.16 mM formate and 4.42 mM acetate. The FDH bearing strain, SBS550MG-Cms243(pHL413KF1) consumed 98.43 mM glucose and produced 171.80 mM succinate, 1 mM formate and 5.78 mM acetate. Furthermore, external formate supplementation to SBS550MG(pHL413KF1) fermentations resulted in about 6% increase in succinate yields as compared to SBS550MG(pHL413Km). In an anaerobic fed-batch bioreactor process, the average glucose consumption rate, succinate productivity, and byproduct formate concentration of SBS550MG(pHL413Km) was 1.40 g/L/h, 1 g/L/h, and 17 mM, respectively. Whereas, the average glucose consumption rate, succinate productivity and byproduct formate concentration of SBS550MG(pHL413KF1) was 2 g/L/h, 2 g/L/h, 0–3 mM respectively. A high cell density culture of SBS550MG(pHL413KF1) showed further improvement in succinate productivity with a higher glucose consumption rate. Reduced levels of byproduct formate in succinate fermentation broth would provide an opportunity for reducing the cost associated with downstream processing, purification, and waste disposal.
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