Mathematical modeling of fluidized-bed c
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L. Zhou; H. Y. Sohn
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Article
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1996
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American Institute of Chemical Engineers
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English
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A mathematical model was formulated to describe the reaction rate and the particle size distribution of solids in a Puidized bed for the chlorination of rutile by a CO/CI, mixture. The bubble assemblage model was applied to describe the gas behaLRor in the bed. The particle-size distribution in the