2001
DOI: 10.1016/s0168-1656(00)00365-5
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Physiological responses to mixing in large scale bioreactors

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Cited by 405 publications
(361 citation statements)
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“…Moreover, installing a functional phosphagen kinase system such as shown here for AK appears to be a pertinent metabolic engineering strategy to improve the biotechnological potential of microbes that are exposed to energetically stressful conditions. One such condition may be large scale processes in which cells are often exposed to fluctuating availability of nutrients such as carbon source and oxygen because of imperfect mixing (44).…”
Section: Discussionmentioning
confidence: 99%
“…Moreover, installing a functional phosphagen kinase system such as shown here for AK appears to be a pertinent metabolic engineering strategy to improve the biotechnological potential of microbes that are exposed to energetically stressful conditions. One such condition may be large scale processes in which cells are often exposed to fluctuating availability of nutrients such as carbon source and oxygen because of imperfect mixing (44).…”
Section: Discussionmentioning
confidence: 99%
“…The results suggested that the production of lactic acid, as the major metabolite influencing the pH change, was also affected by the scaled up conditions in the reactor. It has been frequently reported that scaling up fails to achieve the same results concerning the biomass yield and other metabolites associated with its growth (Enfors et al 2001). Part of the mechanisms responsible for these changes are the different systems of agitation and heating responsible for the homogeneity and the heat distribution in the fermentor (Hewitt and Nienow 2007).…”
Section: Fermentation In a Laboratory Bioreactormentioning
confidence: 99%
“…However, after second-phase addition, the steady-state cell concentration slightly decreased and small amounts of acetate appeared in the medium (results not shown). The presence of the viscous organic phase may have led to incomplete mixing and thus to nonuniform glucose and oxygen concentrations inside the reactor causing acetate formation, as observed in large-scale bioprocesses (17,25,46,62). After the two-liquid-phase culture had attained a steady state, octane was added to the organic phase feed tank (60 mM) and directly into the culture broth to induce styAB expression.…”
Section: Continuous Two-liquid-phase Cultivation Of E Coli Jm101 (Psmentioning
confidence: 99%