M. Rylek
Czechoslovak Academy of Sciences
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Chemical Engineering Science | 1980
František Kaštánek; Jindřich Zahradník; M. Rylek; Jan Kratochvíl
Abstract A simple method is suggested for the modelling of hydrodynamics of reacting gas-liquid systems in large-scale bubble column reactors. Values of liquid-side mass transfer coefficient (kL), interfacial area (a), and gas holdup ratio (e) in a large-scale apparatus can be predicted on the basis of experimental gas holdup data obtained for the reacting system and for an appropriate standard (reference) system in a laboratory-scale bubble reactor. Examples of the modelling are presented for the cases of oxidation of isobutyraldehyde to isobutyric acid and absorption of CO2 into NaOH solution.
Collection of Czechoslovak Chemical Communications | 1984
M. Rylek; Jindřich Zahradník
Chemical Engineering Communications | 1982
Jindřich Zahradník; Jan Kratochvíl; František Kaštánek; M. Rylek
Collection of Czechoslovak Chemical Communications | 1982
Jindřich Zahradník; František Kaštánek; Jan Kratochvíl; M. Rylek
Collection of Czechoslovak Chemical Communications | 1985
Jindřich Zahradník; Jan Kratochvíl; M. Rylek
Collection of Czechoslovak Chemical Communications | 1991
Jindřich Zahradník; M. Rylek
Collection of Czechoslovak Chemical Communications | 1974
Jindřich Zahradník; František Kaštánek; M. Rylek
Collection of Czechoslovak Chemical Communications | 1974
František Kaštánek; Jindřich Zahradník; M. Rylek
Collection of Czechoslovak Chemical Communications | 1977
František Kaštánek; Jan Kratochvíl; M. Rylek
Collection of Czechoslovak Chemical Communications | 1975
M. Rylek; František Kaštánek; L. Nývlt; Jan Kratochvíl