2019
DOI: 10.1002/btpr.2944
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Application of fermentation process control to increase l‐tryptophan production in Escherichia coli

Abstract: In this study, process engineering and process control were applied to increase the production of l‐tryptophan using Escherichia coli Dmtr/pta‐Y. Different dissolved oxygen (DO) and pH control strategies were applied in l‐tryptophan production. DO and pH were maintained at [20% (0–20 hr); 30% (20–40 hr)] and [7.0 (0–20 hr), 6.5 (20–40 hr)], respectively, which increased l‐tryptophan production, glucose conversion percentage [g (l‐tryptophan)/g (glucose)], and transcription levels of key genes for tryptophan bi… Show more

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Cited by 12 publications
(6 citation statements)
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“…Possible modifications to improve L-tryptophan producer strains have been previously summarised by [18,20,[22][23][24][25][26]. High L-tryptophan concentrations of 48.68 g L −1 with glucose as carbon source were reported with rationally engineered E. coli strains [23], and increased titres of 52.57 g L −1 were reached in combination with adapted pH and dissolved oxygen control strategies in the fed-batch process [27]. Aside from high product concentrations, the economic efficiency of production processes is also dependent on substrate conversion rates and the current market values of the carbon sources used.…”
Section: Introductionmentioning
confidence: 99%
“…Possible modifications to improve L-tryptophan producer strains have been previously summarised by [18,20,[22][23][24][25][26]. High L-tryptophan concentrations of 48.68 g L −1 with glucose as carbon source were reported with rationally engineered E. coli strains [23], and increased titres of 52.57 g L −1 were reached in combination with adapted pH and dissolved oxygen control strategies in the fed-batch process [27]. Aside from high product concentrations, the economic efficiency of production processes is also dependent on substrate conversion rates and the current market values of the carbon sources used.…”
Section: Introductionmentioning
confidence: 99%
“…Based on the law of conservation and the pseudo‐steady‐state hypothesis (PSSH) of intracellular intermediate metabolites, a mass metabolic matrix was constructed 28 . A stoichiometric model was assumed to describe the metabolic network of E. coli for L‐threonine production and was constructed on the basis of five assumptions: 23 (a) Cell growth was negligible during the later phase of fermentation; (b) The glyoxylate shunt was considered inactive; (c) There was no transhydrogenase for the interconversion of NADPH and NADH; (d) The stoichiometric matrix was simplified by lumping adjacent reactions lacking branch pathways; and (e) The consumption energy and the maintenance energy were not equivalent due to too much futile energy during the non‐growth period.…”
Section: Methodsmentioning
confidence: 99%
“…The DO, pH, and temperature were automatically measured with electrodes attached to the fermenters. The cell density was measured using a spectrophotometer at 600 nm (OD 600 ), and the OD 600 values and biomass (dry cell weight, DCW) of E. coli were assumed related as: 1 OD 600 = 0.42 g L −1 DCW 28 . The concentration of L‐threonine in the fermentation broth was determined by high‐pressure liquid chromatography using an Agilent 1200 instrument (Agilent Technologies, Santa Clara, CA) 23 .…”
Section: Methodsmentioning
confidence: 99%
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