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Hydrodynamics of two‐phase cocurrent downflow through packed beds. Part I. Macroscopic model
Author(s) -
Rao V. G.,
Ananth M. S.,
Varma Y. B. G.
Publication year - 1983
Publication title -
aiche journal
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.958
H-Index - 167
eISSN - 1547-5905
pISSN - 0001-1541
DOI - 10.1002/aic.690290317
Subject(s) - pressure drop , bubble , mechanics , saturation (graph theory) , drop (telecommunication) , force balance , thermodynamics , chemistry , liquid drop , physics , mathematics , engineering , combinatorics , telecommunications
Abstract Pressure drop and liquid saturation are two important design parameters in cocurrent gas‐liquid downflow through packed beds. A macroscopic model based on momentum balance is formulated for the condition of no radial pressure gradients. The model includes the effect of bubble formation on the pressure drop and holdup and is compared with the experimental data of the earlier investigators and of the present study. The model provides a functional form for correlating pressure drop and liquid saturation but some parameters have to be determined by fitting the experimental data.

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