Engineering Escherichia coli for malate production by integrating modular pathway characterization with CRISPRi-guided multiplexed metabolic tuning

被引:80
|
作者
Gao, Cong [1 ,2 ,3 ]
Wang, Shihui [1 ,2 ,3 ]
Hu, Guipeng [1 ,2 ,3 ]
Guo, Liang [1 ,2 ,3 ]
Chen, Xiulai [1 ,2 ,3 ]
Xu, Peng [4 ]
Liu, Liming [1 ,2 ,3 ]
机构
[1] Jiangnan Univ, State Key Lab Food Sci & Technol, 1800 Lihu Rd, Wuxi 214122, Peoples R China
[2] Jiangnan Univ, Int Joint Lab Food Safety, Wuxi, Peoples R China
[3] Jiangnan Univ, Minist Educ, Key Lab Ind Biotechnol, Wuxi, Peoples R China
[4] Univ Maryland Baltimore Cty, Chem Biochem & Environm Engn, Baltimore, MD 21228 USA
基金
中国国家自然科学基金; 美国国家科学基金会;
关键词
CRISPRi; glyoxylate cycle; in vitro modular optimization; multiplexed combinatorial regulation; IN-VITRO RECONSTITUTION; MALIC-ACID PRODUCTION; SACCHAROMYCES-CEREVISIAE; MEVALONATE PATHWAY; GENE-EXPRESSION; OVERPRODUCTION; PLATFORM; YEAST; BIOSYNTHESIS; OPTIMIZATION;
D O I
10.1002/bit.26486
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
The application of rational design in reallocating metabolic flux to overproduce desired chemicals is always restricted by the native regulatory network. Here, we demonstrated that in vitro modular pathway optimization combined with in vivo multiplexed combinatorial engineering enables effective characterization of the bottleneck of a complex biosynthetic cascade and improves the output of the engineered pathway. As a proof of concept, we systematically identified the rate-limiting step of a five-gene malate biosynthetic pathway by combinatorially tuning the enzyme loads of a reconstituted biocatalytic reaction in a cell-free system. Using multiplexed CRISPR interference, we subsequently eliminated the metabolic constraints by rationally assigning an optimal gene expression pattern for each pathway module. The present engineered strain Escherichia coli B0013-47 exhibited a 2.3-fold increase in malate titer compared with that of the parental strain, with a yield of 0.85 mol/mol glucose in shake-flask culture and titer of 269 mM (36 g/L) in fed-batch cultivation. The strategy reported herein represents a powerful method for improving the efficiency of multi-gene pathways and advancing the success of metabolic engineering.
引用
收藏
页码:661 / 672
页数:12
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