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

被引:81
|
作者
Balzer, Grant J. [1 ]
Thakker, Chandresh [3 ]
Bennett, George N. [3 ]
San, Ka-Yiu [1 ,2 ]
机构
[1] Rice Univ, Dept Bioengn, Houston, TX 77005 USA
[2] Rice Univ, Dept Chem & Biomol Engn, Houston, TX 77005 USA
[3] Rice Univ, Dept Biochem & Cell Biol, Houston, TX 77005 USA
基金
美国国家科学基金会;
关键词
Succinate; Formate; Byproduct; Formate dehydrogenase; NADH; E; coli; PYRUVATE-CARBOXYLASE; CANDIDA-BOIDINII; FERMENTATION; GENE; REDISTRIBUTION; ACID;
D O I
10.1016/j.ymben.2013.07.005
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
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. cob strain SBS550MG-Cms243(pHL413Km). The NAD+-dependent formate dehydrogenase gene (fdh1) of Candida boidinii was coexpressed with Lactococcus tact is pyruvate carboxylase (pycA) under the control of P-trc and P-pycA 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 led 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. (C) 2013 Elsevier Inc. All rights reserved
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页码:1 / 8
页数:8
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