scholarly journals A plug-and-play system for enzyme production at commercially viable levels in fed-batch cultures of Escherichia coli BL21 (DE3)

2018 ◽  
Author(s):  
Sujata Vijay Sohoni ◽  
Paras Harendra Kundalia ◽  
Adarsh G. Shetty ◽  
Avinash Vellore Sunder ◽  
Raghavendra P. Gaikaiwari ◽  
...  

AbstractCommercial exploitation of enzymes in biotransformation necessitates a robust method for enzyme production that yields high enzyme titer. Nitrilases are a family of hydrolases that can transform nitriles to enantiopure carboxylic acids, which are important pharmaceutical intermediates. Here, we report a fed-batch method that uses a defined medium and involves growth under carbon limiting conditions using DO-stat feeding approach combined with an optimized post-induction strategy, yielding high cell densities and maximum levels of active and soluble enzyme. This strategy affords strict control of nutrient feeding and growth rates, and ensures sustained protein synthesis over a longer period. The method was optimized for highest titer of nitrilase reported so far (247 kU/l) using recombinant E. coli expressing the Alcaligenes sp. ECU0401 nitrilase. The fed-batch protocol presented here can also be employed as template to produce a wide variety of enzymes with minimal modification, as demonstrated for alcohol dehydrogenase and formate dehydrogenase.

2013 ◽  
Vol 40 (3-4) ◽  
pp. 335-343 ◽  
Author(s):  
J. Ruiz ◽  
A. Fernández-Castané ◽  
C. de Mas ◽  
G. González ◽  
J. López-Santín

Author(s):  
Quentin Bethune ◽  
Cameron Harrington ◽  
Bhanu Mulukutla

CHO cells have been recently shown to produce amino acid catabolism derived byproducts, which accumulate in fed-batch cultures to growth-inhibitory levels. Residual amino acid limitation or genetic engineering strategies have been successfully employed to suppress production of these novel growth inhibitory metabolic byproducts. However, the growth advantage attained due to suppression of these metabolic byproducts in fed-batch cultures is more pronounced when lactate accumulation is also controlled. BCAT1 knock-out (KO) CHO cells, which produce negligible levels of the metabolic byproducts isovalerate, isobutyrate and 2-methylbutyrate, grow to significantly higher peak cell densities in fed-batch cultures with lactate control (HiPDOG) as compared to cultures without lactate control. Henceforth, strategies involving novel metabolic byproduct control should preferably include lactate control to more easily assess the enhanced cell growth and productivities attainable.


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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