Enhanced production of N-acetyl-D-neuraminic acid by multi-approach whole-cell biocatalyst

被引:45
|
作者
Lin, Bai-Xue [1 ]
Zhang, Zi-Juan [1 ]
Liu, Wei-Feng [1 ]
Dong, Zhi-Yang [2 ]
Tao, Yong [1 ]
机构
[1] Chinese Acad Sci, Inst Microbiol, Dept Ind Microbiol & Biotechnol, Beijing 100101, Peoples R China
[2] Chinese Acad Sci, Inst Microbiol, State Key Lab Microbial Resources, Beijing 100101, Peoples R China
基金
中国科学院院长基金特别;
关键词
N-Acetyl-D-neuraminic acid; Escherichia coli; Metabolic engineering; Whole-cell biocatalyst; Biotransformation; D-GLUCOSAMINE; 2-EPIMERASE; SIALIC-ACID; ESCHERICHIA-COLI; ACETYLNEURAMINIC ACID; CHEMOENZYMATIC SYNTHESIS; COLOMINIC ACID; ACETYLGLUCOSAMINE; BIOSYNTHESIS; OPTIMIZATION; PATHWAY;
D O I
10.1007/s00253-013-4754-8
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
N-Acetyl-d-neuraminic acid (Neu5Ac) has attracted considerable interest due to its promising potential applications in medicine. Significant efforts have been made in whole-cell biocatalyst for Neu5Ac production, but the processes often result in suboptimal performance due to poor expression of enzymes, imbalances of pathway components, disturbance of competing pathways, and barriers of mass transport. In this study, we engineered Escherichia coli strains capable of producing Neu5Ac by assembling a two-step heterologous pathway consisting of N-acetyl-d-glucosamine 2-epimerase (AGE) and Neu5Ac aldolase (NanA). Multiple approaches were used to improve the efficiency of the engineered pathway and process for enhanced Neu5Ac production. Firstly, we identified that NanA was the rate-controlling enzyme in this pathway. With increased expression of NanA, a ninefold increase in Neu5Ac production (65 mM) was observed. Secondly, knocking out nanTEK genes blocked Neu5Ac uptake and the competing pathway, which kept the reactions to the synthetic direction as the final product went outside of the cells and enhanced the Neu5Ac production by threefold, resulting in 173.8 mM of Neu5Ac. Thirdly, we improved the performance of the system by promoting substrate transport and optimizing concentrations of substrates. An overall whole-cell biocatalytic process was developed and a maximum titer of 240 mM Neu5Ac (74.2 g/L) was achieved, with productivity of 6.2 g Neu5Ac/L/h and conversion yield of 40 % from GlcNAc. The engineered strain could be reused for at least five cycles with a productivity of > 6 g/L/h. It is a cost-effective process for Neu5Ac production with potential applications in large-scale industrial production.
引用
收藏
页码:4775 / 4784
页数:10
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