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Unsaturated liquid percolation flow through nonwetted packed beds
Author(s) -
Liu D. Y.,
Wang G. X.,
Litster J. D.
Publication year - 2002
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.690480505
Subject(s) - reynolds number , packed bed , percolation (cognitive psychology) , particle (ecology) , dispersion (optics) , flow (mathematics) , materials science , spheres , volumetric flow rate , mechanics , particle size , liquid flow , wax , range (aeronautics) , chemistry , chromatography , composite material , optics , physics , turbulence , geology , oceanography , astronomy , neuroscience , biology
The unsaturated flow of liquid through packed beds of large particles was studied using six different liquids, all with contact angles greater than 90° on the bed packing (wax spheres of 9, 15 and 19.4 mm diameter). The liquidflow was discrete in nature, as drops for low flow rates and rivulets for high flow rates. For unsaturated liquid flows, the actual percolation velocity, not superficial velocity, should be used to characterize the flow. The percolation velocity did not vary with packed‐bed depth, but was a strong function of liquid flow rate, liquid and particle properties. Effects of liquid and particle properties (but not flow rate) are well captured by a simple correlation between the liquid‐particle fiction factor and Reynolds number based on actual percolation velocities. Liquid dispersion, characterized by the maximum dispersion angle, varies significantly with liquid and particle properties. The tentative correlation suggested here needs further validation for a wider range of conditions.