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A model for flow regime transitions in cocurrent down‐flow trickle‐bed reactors
Author(s) -
Ng K. M.
Publication year - 1986
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.690320113
Subject(s) - trickle , trickle bed reactor , flow (mathematics) , porosity , mechanics , surface tension , volumetric flow rate , viscosity , thermodynamics , materials science , chemistry , catalysis , physics , computer science , composite material , biochemistry , world wide web
A study of the nature of interstitial flows within trickle‐bed reactors is presented. Based on physical concepts, a theory is developed to predict the transition boundaries for various flow regimes for nonfoaming liquids. The effects of factors such as bed porosity, size of monodispersed spherical catalyst particles, interfacial tension, viscosity, density, and the gas and liquid flow rates, on flow transitions are considered. Experimental data in the literature are used to confirm the theory and the agreement is good.