Hydrodynamics of the cocurrent downflow of a gas and a foaming liquid through a packed bed. Part I. Estimation of the transition boundary between the hydrodynamic regimes from the gas continuous flow to the pulsing flow
- 29 February 2004
- journal article
- Published by Elsevier BV in Chemical Engineering and Processing - Process Intensification
- Vol. 43 (2), 169-179
- https://doi.org/10.1016/s0255-2701(03)00004-7
Abstract
No abstract availableKeywords
This publication has 28 references indexed in Scilit:
- Multiphase catalytic reactors: a perspective on current knowledge and future trendsCatalysis Reviews, 2002
- TRICKLE BED REACTORSReviews in Chemical Engineering, 1996
- Purification of exhaust air containing organic pollutants in a trickle-bed bioreactor.Applied Microbiology and Biotechnology, 1991
- Pressure drop in gas‐liquid downflow through packed bedsAIChE Journal, 1987
- Flow patterns and some holdup experimental data in trickle‐bed reactors for foaming, nonfoaming, and viscous organic liquidsAIChE Journal, 1978
- Two‐phase downflow through catalyst beds: Part I. Flow mapsAIChE Journal, 1977
- Flow pattern, pressure loss and liquid holdup data in gas-liquid downflow packed beds with foaming and nonfoaming hydrocarbons.JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1976
- Some liquid holdup experimental data in trickle‐bed reactors for foaming and nonfoaming hydrocarbonsAIChE Journal, 1975
- Fluid‐flow characteristics of concurrent gas‐liquid flow in packed bedsAIChE Journal, 1964
- Two‐phase concurrent flow in packed bedsAIChE Journal, 1961