Article ID Journal Published Year Pages File Type
238115 Powder Technology 2009 11 Pages PDF
Abstract

Semi-fluidized bed hydrodynamics, including minimum and maximum semi-fluidization velocities, packed bed formation and pressure drop across the bed, have been studied in a 0.1 m ID liquid–solid semi-fluidized bed. The top grid is a specially designed perforated plate to have negligible pressure drop across it and to retain all the particles used in the experiment. Experimental parameters studied included velocity, density and viscosity of the liquid, particle size, static bed height and expansion ratio. Empirical and semi-empirical models have been derived. The results have been compared with those available in the literature.

Graphical abstractSemi-fluidized bed hydrodynamics, including minimum and maximum semi-fluidization velocities, packed bed formation and pressure drop across the bed, have been studied. The effect of the system parameters like; velocity, density and viscosity of the liquid, particle size, static bed height and expansion ratio has been discussed. Empirical and semi-empirical models have been derived.Figure optionsDownload full-size imageDownload as PowerPoint slide

Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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