Fed-batch two-phase production of alanine by a metabolically engineered Escherichia coli

2006 ◽  
Vol 28 (20) ◽  
pp. 1695-1700 ◽  
Author(s):  
Geoffrey M. Smith ◽  
Sarah A. Lee ◽  
Kevin C. Reilly ◽  
Mark A. Eiteman ◽  
Elliot Altman
2011 ◽  
Vol 10 (1) ◽  
pp. 59 ◽  
Author(s):  
Hui-Jeong Jang ◽  
Sang-Hwal Yoon ◽  
Hee-Kyung Ryu ◽  
Jung-Hun Kim ◽  
Chong-Long Wang ◽  
...  

Molecules ◽  
2021 ◽  
Vol 26 (23) ◽  
pp. 7173
Author(s):  
Tao Cheng ◽  
Xiuhong Liang ◽  
Yaqun Wang ◽  
Ningning Chen ◽  
Dexin Feng ◽  
...  

Lactate and isoprene are two common monomers for the industrial production of polyesters and synthetic rubbers. The present study tested the co-production of D-lactate and isoprene by engineered Escherichia coli in microaerobic conditions. The deletion of alcohol dehydrogenase (adhE) and acetate kinase (ackA) genes, along with the supplementation with betaine, improved the co-production of lactate and isoprene from the substrates of glucose and mevalonate. In fed-batch studies, microaerobic fermentation significantly improved the isoprene concentration in fermentation outlet gas (average 0.021 g/L), compared with fermentation under aerobic conditions (average 0.0009 g/L). The final production of D-lactate and isoprene can reach 44.0 g/L and 3.2 g/L, respectively, through fed-batch microaerobic fermentation. Our study demonstrated a dual-phase production strategy in the co-production of isoprene (gas phase) and lactate (liquid phase). The increased concentration of gas-phase isoprene could benefit the downstream process and decrease the production cost to collect and purify the bio-isoprene from the fermentation outlet gas. The proposed microaerobic process can potentially be applied in the production of other volatile bioproducts to benefit the downstream purification process.


RSC Advances ◽  
2018 ◽  
Vol 8 (54) ◽  
pp. 30851-30859
Author(s):  
Chang Qi ◽  
Hongwei Zhao ◽  
Wenyang Li ◽  
Xing Li ◽  
Haiying Xiang ◽  
...  

A sustainable technology for gamma (γ)-terpinene was constructed in an engineered Escherichia coli. In-depth analysis at translation level for the engineered strain and intermediate metabolites were analyzed. The fed-batch fermentation of γ-terpinene was 275.41 mg L−1.


2016 ◽  
Vol 5 (11) ◽  
pp. 1299-1307 ◽  
Author(s):  
Yunjie Li ◽  
Bing Huang ◽  
Hui Wu ◽  
Zhimin Li ◽  
Qin Ye ◽  
...  

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