scholarly journals Differential expression of small RNAs under chemical stress and fed-batch fermentation in E. coli

BMC Genomics ◽  
2015 ◽  
Vol 16 (1) ◽  
Author(s):  
Martin Holm Rau ◽  
Klara Bojanovič ◽  
Alex Toftgaard Nielsen ◽  
Katherine S. Long
2014 ◽  
Vol 989-994 ◽  
pp. 997-1002 ◽  
Author(s):  
Jian Wang ◽  
Jia Kai Sun ◽  
Qing Yang Xu

Metabolic engineering ofCorynebacterium glutamicumhas sought to divert carbon into L-isoleucine. However, the fermentation period of this strain is long. TheC.glutamicumYILW strain (LeuL, AHVr, SGr, Leu-MEr) was previously derived by repeated compound mutagenesis which could accumulate 20.2 g/L L-isoleucine in a 5-L jar fermentor. Overexpression of the threonine dehydratase gene (ilvA) fromCorynebacterium glutamicumYILW and coexpression of threonine dehydratase and acetolactate synthase (ilvBN) from it were employed to divert carbon flux toward L-isoleucine. The strainE. coliTRFC with the expression ofilvA could accumulate L-isoleucine of 6.8 g/L without accumulation of any L-threonine by fed-batch fermentation in a 5-L jar fermentor. However, the production of L-isoleucine by the strainE.coliTRFC with the co-expression ofilvA andilvBN was decreased by 19.1%, and the production of L-valine was increased by 40% compared with that ofE. coliTRFC with the expression ofilvA.


2000 ◽  
Vol 22 (5) ◽  
pp. 379-383 ◽  
Author(s):  
A. K. Panda ◽  
R. H. Khan ◽  
S. Mishra ◽  
K. B. C. Appa Rao ◽  
S. M. Totey

2021 ◽  
Vol 20 (1) ◽  
Author(s):  
Michael Sibley ◽  
John M. Ward

Abstract Background A fundamental problem associated with E. coli fermentations is the difficulty in achieving high cell densities in batch cultures, attributed in large part to the production and accumulation of acetate through a phenomenon known as overflow metabolism when supplying enough glucose for the cell density desired. Although a fed-batch configuration is the standard method for reducing such issues, traditional fed-batch systems require components which become problematic when applying them at smaller scale. One alternative has been the development of a system whereby the enzymatic degradation of starch is used to release glucose at a controlled rate. However, to date, amylolytic enzymes have only been applied to the culture exogenously, whereas our goal is to design and construct a self-secreting amylolytic chassis capable of self-regulated enzyme-based fed-batch fermentation. Results A putative glucoamylase from C. violaceum has been cloned and expressed in E. coli BL21(DE3) and W3110, which exhibits significant glucose releasing amylolytic activity. Extracellular amylolytic activity was enhanced following a replacement of the enzymes native signal peptide with the DsbA signal sequence, contributing to a glucoamylase secreting strain capable of utilising starch as a sole carbon source in defined media. Introduction of PcstA, a glucose sensitive K12 compatible promoter, and the incorporation of this alongside C. violaceum glucoamylase in E. coli W3110, gave rise to increased cell densities in cultures grown on starch (OD600 ∼ 30) compared to those grown on an equivalent amount of glucose (OD600 ∼ 15). Lastly, a novel self-secreting enzyme-based fed-batch fermentation system was demonstrated via the simultaneous expression of the C. violaceum glucoamylase and a recombinant protein of interest (eGFP), resulting in a fourfold increase in yield when grown in media containing starch compared with the glucose equivalent. Conclusions This study has developed, through the secretion of a previously uncharacterised bacterial glucoamylase, a novel amylolytic E. coli strain capable of direct starch to glucose conversion. The ability of this strain to achieve increased cell densities as well as an associated increase in recombinant protein yield when grown on starch compared with an equivalent amount of glucose, demonstrates for the first time a cell engineering approach to enzyme-based fed-batch fermentation.


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