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Correlating gas–liquid co‐current flow hydrodynamics in packed beds using the F ‐function concept
Author(s) -
Radilla Giovanni,
Fourar Mostafa,
Larachi Faiçal
Publication year - 2005
Publication title -
journal of chemical technology and biotechnology
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.64
H-Index - 117
eISSN - 1097-4660
pISSN - 0268-2575
DOI - 10.1002/jctb.1147
Subject(s) - pressure drop , saturation (graph theory) , packed bed , bubble , mechanics , two phase flow , current (fluid) , thermodynamics , flow (mathematics) , power law , pressure gradient , liquid phase , power function , liquid flow , materials science , chemistry , mathematics , physics , chromatography , mathematical analysis , statistics , combinatorics
A phenomenological model based on the generalization of the single‐phase Forchheimer equation was recently proposed for predicting pressure drop and phase saturations in gas–liquid co‐current horizontal and downward high‐pressure packed beds. Here, we extend the model to packed‐bubble (co‐current upflow) and trickle‐bed operation using phase saturation power laws similar to Corey relative permeabilities. The power‐law exponents were fitted using a wide pressure gradient and liquid saturation databank in co‐current up/downward packed‐bed flows. It was found that this approach, as well as other in the literature developed for down‐flow reactors apply also to upward flows; the prediction accuracy was comparable for both flow directions to existing literature approaches. Copyright © 2004 Society of Chemical Industry