Collect. Czech. Chem. Commun.
1975, 40, 3130-3144
https://doi.org/10.1135/cccc19753130
The hydrodynamics and mass transfer in a packed bubble bed column
V. Pexidr and J. C. Charpentier
Crossref Cited-by Linking
- Abraham M., Sawant S.B.: Hydrodynamics and mass transfer characteristics of packed bubble columns. The Chemical Engineering Journal 1990, 43, 95. <https://doi.org/10.1016/0300-9467(90)80011-Z>
- Oyevaar M.H., de la Rie T., van der Sluijs C.L., Westerterp K.R.: Interfacial areas and gas hold-ups in bubble columns and packed bubble columns at elevated pressures. Chemical Engineering and Processing: Process Intensification 1989, 26, 1. <https://doi.org/10.1016/0255-2701(89)87001-1>
- Gestrich Wolfgang, Harth Hubert: Flüssigphase‐Rückvermischung in gepackten Blasensäulen. Chemie Ingenieur Technik 1981, 53, 308. <https://doi.org/10.1002/cite.330530503>
- Turek Fritz, Lange Rüdiger: Mass transfer in trickle-bed reactors at low reynolds number. Chemical Engineering Science 1981, 36, 569. <https://doi.org/10.1016/0009-2509(81)80145-5>
- Botton R., Cosserat D., Charpentier J.C.: Mass transfer in bubble columns operating at high gas throughputs. The Chemical Engineering Journal 1980, 20, 87. <https://doi.org/10.1016/0300-9467(80)85029-5>
- Sawant S.B., Pangarkar V.G., Joshi J.B.: Gas hold-up and mass transfer characteristics of packed bubble columns. The Chemical Engineering Journal 1979, 18, 143. <https://doi.org/10.1016/0300-9467(79)80024-6>
- Botton R., Cosserat D., Charpentier J.C.: Influence of column diameter and high gas throughputs on the operation of a bubble column. The Chemical Engineering Journal 1978, 16, 107. <https://doi.org/10.1016/0300-9467(78)80051-3>
- Charpentier J.C.: Recent progress in two phase gas—liquid mass transfer in packed beds. The Chemical Engineering Journal 1976, 11, 161. <https://doi.org/10.1016/0300-9467(76)80038-X>