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Flow structure of the solids in gas-solid fluidized beds
Authors:Navid Mostoufi
Affiliation:a Process Design and Simulation Research Centre, Department of Chemical Engineering, Faculty of Engineering, University of Tehran, P.O. Box 11365/4563, Tehran, Iran
b Department of Chemical Engineering, École Polytechnique de Montréal, P.O. Box 6079, Succ. Station Centre-Ville, Montréal, Qué., Canada H3C 3A7
Abstract:Existence of clusters in dense fluidized beds was investigated by analyzing the time-position data of a tracer obtained in several radioactive particle tracking experiments. It was found that in the case of sand particles, more gas passes through the bed as bubbles with increasing the superficial gas velocity and in the case of FCC powder, flow of the gas through the bed as bubbles does not increase in the turbulent fluidization regime. Cluster diameters were estimated from their velocities and found that descending clusters are generally larger than ascending ones and the size of both increases with increasing the superficial gas velocity. Bubble velocities evaluated in this work are in good agreement with the correlations in the bubbling regime of the fluidization available in the literature.
Keywords:Fluidization   Hydrodynamics   Multiphase flow   Powder technology   Cluster   Particle tracking
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