Department of Bioengineering, Rice University, Houston, TX 77005, USA.
Metab Eng. 2013 Nov;20:1-8. doi: 10.1016/j.ymben.2013.07.005. Epub 2013 Jul 20.
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, 1mM 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, 1g/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.
琥珀酸是一种特殊化学品,在工业、制药和食品用途中有多种应用。琥珀酸发酵过程中的主要挑战之一是消除副产物的形成。在这项研究中,我们通过对高产琥珀酸的大肠杆菌 SBS550MG-Cms243(pHL413Km)菌株进行工程改造,描述了消除副产物甲酸盐并提高琥珀酸产量的方法。我们共表达了 Candida boidinii 的 NAD(+)-依赖性甲酸盐脱氢酶基因(fdh1)和 Lactococcus lactis 的丙酮酸羧化酶(pycA),受 Ptrc 和 PpycA 启动子的控制,位于质粒 pHL413KF1 中。新引入的 fdh1 将 1 摩尔甲酸盐转化为 1 摩尔 NADH 和 CO2。工程改造后的菌株 SBS550MG-Cms243(pHL413KF1)通过增加 NADH 的可用性来保留甲酸盐的还原能力。在厌氧摇瓶发酵中,亲本菌株 SBS550MG-Cms243(pHL413Km)消耗了 99.86 mM 葡萄糖,产生了 172.38 mM 琥珀酸、16.16 mM 甲酸盐和 4.42 mM 乙酸盐。携带 FDH 的菌株 SBS550MG-Cms243(pHL413KF1)消耗了 98.43 mM 葡萄糖,产生了 171.80 mM 琥珀酸、1 mM 甲酸盐和 5.78 mM 乙酸盐。此外,向 SBS550MG(pHL413KF1)发酵液中补充外源甲酸盐可使琥珀酸产量提高约 6%,与 SBS550MG(pHL413Km)相比。在厌氧分批补料生物反应器过程中,SBS550MG(pHL413Km)的平均葡萄糖消耗速率、琥珀酸生产力和副产物甲酸盐浓度分别为 1.40 g/L/h、1 g/L/h 和 17 mM。然而,SBS550MG(pHL413KF1)的平均葡萄糖消耗速率、琥珀酸生产力和副产物甲酸盐浓度分别为 2 g/L/h、2 g/L/h 和 0-3 mM。高细胞密度培养 SBS550MG(pHL413KF1)可进一步提高琥珀酸生产力,同时提高葡萄糖消耗速率。琥珀酸发酵液中副产物甲酸盐水平的降低将为降低与下游加工、纯化和废物处理相关的成本提供机会。