Effect of column inclination on the performance of three‐phase fluidized beds
- 1 August 1992
- journal article
- Published by Wiley in AIChE Journal
- Vol. 38 (8) , 1206-1212
- https://doi.org/10.1002/aic.690380808
Abstract
No abstract availableKeywords
This publication has 8 references indexed in Scilit:
- Modeling of particle—liquid heat and mass transfer in multiphase systems with the film—penetration modelChemical Engineering Science, 1993
- Gas holdup in three-phase immobilized-cell bioreactorsApplied Biochemistry and Biotechnology, 1990
- Particle-to-liquid mass transfer in gas-liquid-solid fluidization.JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1988
- Solid-liquid mass transfer in three-phase fixed and fluidized bedsChemical Engineering Science, 1987
- Dispersion coefficients for ideal bubbly flow in truly vertical bubble columnsChemical Engineering Science, 1987
- Gas‐liquid mass transfer in fluidized particle bedsAIChE Journal, 1985
- Effect of liquid depth, column inclination and baffle plates on gas holdup in bubble columns.JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1985
- Simultaneous measurement of interfacial area and mass transfer coefficient in three-phase fluidized bedsAIChE Journal, 1980