Dynamic pressure method for kla measurement in large‐scale bioreactors
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[1] V. Linek,et al. Chemical Engineering Use of Catalyzed Sulfite Oxidation Kinetics for the Determination of Mass Transfer Characteristics of Gas-Liquid Contactors , 1981 .
[2] W.-D. Deckwer,et al. Analysis of chemical methods for determination of interfacial areas in gas-in-liquid dispersions with non-uniform bubble sizes , 1980 .
[3] André Laurent,et al. Limits of the chemical method for the determination of physical mass transfer parameters in mechanically agitated gas‐liquid reactors , 1980 .
[4] M. Oyevaar,et al. Interfacial Areas and Gas Hold-ups at Elevated Pressures in a Mechanically Agitated Gas-Liquid Reactor , 1988 .
[5] V. Linek,et al. An experimental study of oxygen probe linearity and transient characteristics in the high oxygen concentration range , 1984 .
[6] P. Beneš,et al. A critical review and experimental verification of the correct use of the dynamic method for the determination of oxygen transfer in aerated agitated vessels to water, electrolyte solutions and viscous liquids , 1987 .
[7] V. Linek,et al. The role of interphase nitrogen transport in the dynamic measurement of the overall volumetric mass transfer cefficient in air‐sparged systems , 1981 .
[8] V. Linek,et al. The chemical method for the determination of the interfacial area: The influence of absorption rate on the hold-up and on the interfacial area in a heterogeneous gas—liquid system , 1969 .