2010
DOI: 10.1016/j.ymben.2009.07.006
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Application of dynamic flux balance analysis to an industrial Escherichia coli fermentation

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Cited by 106 publications
(80 citation statements)
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“…The biomass mass transfer coefficients k X (0) were tuned such that steady-state, mature biofilms would have biomass concentrations within published ranges [13]. Due to the lack of experimentally determined values for B. thetaiotaomicron and F. prausnitzii, glucose and amino acid maximum uptake rates v max reported for E. coli [70] were used for all three species. All byproducts were assumed to have the same v max values as glucose.…”
Section: Model Parameterization and Solutionmentioning
confidence: 99%
See 1 more Smart Citation
“…The biomass mass transfer coefficients k X (0) were tuned such that steady-state, mature biofilms would have biomass concentrations within published ranges [13]. Due to the lack of experimentally determined values for B. thetaiotaomicron and F. prausnitzii, glucose and amino acid maximum uptake rates v max reported for E. coli [70] were used for all three species. All byproducts were assumed to have the same v max values as glucose.…”
Section: Model Parameterization and Solutionmentioning
confidence: 99%
“…All byproducts were assumed to have the same v max values as glucose. Furthermore, all nutrients and byproducts were assumed to have the same Michaelis-Menten constants K m as reported for glucose uptake in E. coli [70]. Planktonic experiments could be conducted to estimate these uptake kinetic parameters, although different parameter values may be appropriate under biofilm conditions.…”
Section: Model Parameterization and Solutionmentioning
confidence: 99%
“…The core of the models was a genome-scale constraint-based metabolic model of S. cerevisiae (Herrgård et al 2008;Jouhten et al 2012;Aung et al 2013). dFBA has been shown to successfully approximate culture dynamics over a longer time scale when the extracellular culture dynamics are magnitudes slower than the intracellular metabolic dynamics (Varma and Palsson 1994;Mahadevan et al 2002;Sainz et al 2003;Hjersted and Henson 2009;Meadows et al 2010;Jouhten et al 2012). This is often the case since microbes tend to strive for steady-state metabolism to maintain intracellular homeostasis.…”
Section: Dynamic Flux Balance Analysismentioning
confidence: 99%
“…However, we also note that the coefficient of KNO C2 is slightly negative (À0.018) which means that removal of competitive pathways (i.e., genetic knockout) may not successfully improve the biosynthesis yield. While this conclusion seems highly uncertain ( P-value ¼ 0.88; standard error ¼ 0.11), it has been shown via in silico analysis that knockout strategies cannot ensure the improvement for product yield even though it is expected to channel more carbon to the final product (Blazeck and Alper, 2010;Boghigian et al, 2010;Feist et al, 2010;Meadows et al, 2010). This inconsistency can be attributed to unfavorable metabolite accumulation and low capacity of biosynthesis pathways for flux amplification after removal of competitive pathways.…”
Section: à0018mentioning
confidence: 99%
“…To this end, systems biology-based models have been developed to provide useful information for rationally engineering microbial hosts with the desired phenotype as well as to design optimal fermentation conditions (Blazeck and Alper, 2010;Boghigian et al, 2010;Feist et al, 2010;Meadows et al, 2010). Cell-wide metabolic analysis via fluxomics and metabolic control theories are often used to estimate metabolic potential, product yield, nutrient limitations, and gene targets for metabolic engineering (Feist et al, 2010;Wildermuth, 2000).…”
Section: Introductionmentioning
confidence: 99%