Chemical Engineering Communications · 1989 · 192 citations · 31 references
EngineeringChemical EngineeringColloid ScienceFluid DynamicsFluid MechanicsPacked Bed FlowParticle-laden FlowsFluidized Bed HydrodynamicsParticle Settling BehaviorParticle SuspensionsSedimentation VelocitySettling CharacteristicsSuspensionsWall EffectsWall Slip Effects
Abstract The published correlations for the velocity-voidage relationship observed during fluidization and sedimentation of uniformly sized spherical particles in solid-liquid systems are compared with published experimental results. It is found that the expression suggested by Richardson and Zaki represents the experimental data well over a wide range of values of Galileo number (10−2 < Ga< 1010) and voidage (0·4 < ϵ < 1). Methods are given for predicting the constants in the expression as a function of the properties of the system, including wall effects. KEYWORDS: Fluidized bedsFluid-particle interactionsSpherical particles. Additional informationNotes on contributorsA.R. KHAN Present address: Department of Chemical Engineering, University of Technology, Loughborough, Leicestershire, LEU 3TU, UK.
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Fluid Flow Through Packed Columns
Şule Ergün · Medical Entomology and Zoology · 1952 · 7K citations
Low Reynolds Number Hydrodynamics
J. R. A. Pearson · Chemical Engineering Science · 1966 · 1.7K citations