Title of article :
Mixing and drift in gas-fluidised beds
Author/Authors :
Eames، نويسنده , , I. and Gilbertson، نويسنده , , M.A.، نويسنده ,
Issue Information :
روزنامه با شماره پیاپی سال 2005
Pages :
9
From page :
185
To page :
193
Abstract :
One of the most important aspects of bubbling fluidised beds is the mixing they promote. Rowe et al. demonstrated experimentally that the dominant mechanisms of mixing in the bulk of the bed are drift, or permanent displacement of particles, induced by the bubbles, and the return flow it generates [P. Rowe, B. Partridge, A. Cheney, G. Henwood, E. Lyall, The mechanics of solids mixing in fluidised beds, Trans. Inst. Chem. Eng. 43 (1965) 271–286] [1]. We show how, by combining new results relating drift and dispersion, practical estimates of mixing rates consistent with Roweʹs view of mixing can be obtained [P. Rowe, B. Partridge, A. Cheney, G. Henwood, E. Lyall, The mechanics of solids mixing in fluidised beds, Trans. Inst. Chem. Eng. 43 (1965) 271–286] [1]. We also develop Batchelorʹs vortex model of bubbles in fluidised beds to elucidate aspects of bubble structure.
Keywords :
bubbles , drift , Vortices , Modelling , Mixing , Fluidisation
Journal title :
Powder Technology
Serial Year :
2005
Journal title :
Powder Technology
Record number :
1695322
Link To Document :
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