Influence of viscosity on gas holdup formation in stirred tank reactors

Author:

Kracík TomášORCID,Moucha Tomáš

Publisher

Springer Science and Business Media LLC

Subject

Materials Chemistry,Industrial and Manufacturing Engineering,General Chemical Engineering,Biochemistry,General Chemistry

Reference15 articles.

1. Abrardi V, et al (1988) Sparged vessels agitated by multiple turbines. In: 6th European conference on mixing. BHRA the fluid engineering centre: Pavia. pp. 329-336

2. Bouaifi M et al (2001) A comparative study of gas hold-up, bubble size, interfacial area and mass transfer coefficients in stirred gas–liquid reactors and bubble columns. Chem Eng Process 40(2):97–111

3. Calderbank PH (1958) Physical rate processes in industrial fermentation, Part I: the interfacial area in gas-liquid contacting with mechanical agitation. Trans Inst Chem Engrs 36:443–463

4. Foust H, Mack D, Rushton J (1944) Gas-liquid contacting by mixers. Ind Eng Chem 36(6):517–522

5. Kracík T (2014) Optimalizace provozu fermentoru s mechanickými míchadly: poloprovozní měření. Department of Chemical Engineering. University of chemistry and Technology, Prague

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