Liquid holdup and dispersion in packed columns
- 1 January 1990
- journal article
- research article
- Published by Elsevier in Chemical Engineering Science
- Vol. 45 (3) , 759-763
- https://doi.org/10.1016/0009-2509(90)87017-m
Abstract
No abstract availableThis publication has 13 references indexed in Scilit:
- A residence‐time model for trickle‐flow reactors incorporating incomplete mixing in stagnant regionsAIChE Journal, 1983
- Gas‐liquid reactions in packed beds: The effectiveness of static hold‐up in presence of gas side resistanceThe Canadian Journal of Chemical Engineering, 1981
- MASS TRANSFER COEFFICIENT BETWEEN THE STATIC AND DYNAMIC HOLD-UPS IN A PACKED COLUMN∗Chemical Engineering Communications, 1981
- Gas‐Liquid reactions in packed beds: Regimes of reaction in the static hold‐upThe Canadian Journal of Chemical Engineering, 1980
- The effectiveness of static hold‐up for absorption with a chemical reaction in a packed trickle bed: General order kineticsThe Canadian Journal of Chemical Engineering, 1979
- Gas liquid reactions in a packed bed: Some implications of the extended crossflow modelThe Canadian Journal of Chemical Engineering, 1978
- Effective interfacial area in packed beds for absorption with chemical reactionThe Canadian Journal of Chemical Engineering, 1978
- Longitudinal Dispersion in Packed Gas-Absorption ColumnsIndustrial & Engineering Chemistry Fundamentals, 1977
- Axial mixing of liquid in gas‐liquid flow through packed bedsThe Canadian Journal of Chemical Engineering, 1965
- Axial dispersion of mass in flow through fixed bedsAIChE Journal, 1958