František Kaštánek
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.
Archive | 1992
František Kaštánek; Jindřich Zahradník
Collection of Czechoslovak Chemical Communications | 1987
Jindřich Zahradník; Rudolf Peter; František Kaštánek
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 | 1982
Jindřich Zahradník; František Kaštánek; Jan Kratochvíl
Collection of Czechoslovak Chemical Communications | 1978
Jindřich Zahradník; František Kaštánek
Collection of Czechoslovak Chemical Communications | 1979
Jan Čermák; František Kaštánek; Antonín Havlíček
Collection of Czechoslovak Chemical Communications | 1974
Jindřich Zahradník; František Kaštánek; M. Rylek
Collection of Czechoslovak Chemical Communications | 1989
Jan Kratochvíl; František Kaštánek
