1994
DOI: 10.1002/bit.260440819
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Characterization of mixing in stirred tank bioreactors equipped with rushton turbines

Abstract: Microbial conversions involve multiphase systems with many different interactions, i.e., cellular reactions, gasliquid mass transfer, liquid mixing, and substrate diffusion into cell aggregates.6 A complete quantitative description of a bioprocess requires the fitting together of pieces of modelling, and the final model for the whole system may be very complex. In an attempt to reduce the interactions in the model, one normally studies the effect of different mechanisms separately. Thus, microbial kinetics is … Show more

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Cited by 17 publications
(5 citation statements)
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“…has described¯uorescence studies with a 30 dm 3 fermenter, and Namdev et al Fluid mixing is important in bioreactors because incomplete mixing generates non-uniform spatial distributions of cells, substrates and products. These non-uniformities can have profound effects on the relative growth rates of competing species, 6 the rates of oxygen uptake, 7 and the stability of the reactor.…”
Section: Notationmentioning
confidence: 98%
“…has described¯uorescence studies with a 30 dm 3 fermenter, and Namdev et al Fluid mixing is important in bioreactors because incomplete mixing generates non-uniform spatial distributions of cells, substrates and products. These non-uniformities can have profound effects on the relative growth rates of competing species, 6 the rates of oxygen uptake, 7 and the stability of the reactor.…”
Section: Notationmentioning
confidence: 98%
“…Cooke et al (1988) used 0.4% CMC solutions to quantify k L a inside 4 m 3 bioreactors, and proposed a correlation to predict k L a , including a surprisingly strong effect of the viscosity: k L a ∝ µ −1 . Several studies have also been done with XG solutions (Pedersen et al, 1994; Garcia‐Ochoa and Gomez, 1998) inside small reactors of less than 25 L. Herbst et al (1992) studied XG production inside 0.2–3 m 3 reactors by oxygen mass balance and validated the correlation of Kawase and Moo‐Young (1988) at different scales. This is a very interesting study reports a strong effect of the choice of impellers but it covers a specific range of rheology and operating conditions, as it focuses on very high XG concentrations—up to 2%—and only one gas flow rate.…”
Section: Introductionmentioning
confidence: 96%
“…Fibre suspensions have also been used for their filamentous structure (Cooke et al, 1988; Dronawat et al, 1997; Benchapattarapong et al, 2005), despite possible difficulties in mimicking the real rheology of highly shear‐thinning filamentous fungi. Model fluids are also used for the study of mixing time and power consumption in viscous media (Luong and Volesky, 1979; Nienow and Elson, 1988; Henzler and Obernosterer, 1991; Pedersen et al, 1993, 1994; Nienow et al, 1996; Vlaev et al, 2002; Albaek et al, 2008). A detailed discussion on rheological measurements of mycelial broth and model media is proposed by various authors (Metz and Kossen, 1977; Metz et al, 1979; Kim et al, 1983; Allen and Robinson, 1990; Olsvik and Kristiansen, 1994; Svihla et al, 1997).…”
Section: Introductionmentioning
confidence: 99%
“…Much of the most important work on stirred tank hydrodynamics has been devoted to the choice of an appropriate impeller or combination of impellers to maximize mixing and mass transfer on a global scale . Because of the difficulties of studying biological media, model fluids have often been chosen as they are cheaper and easier to use.…”
Section: Introductionmentioning
confidence: 99%