Flow structure of the solids in gas-solid fluidized beds

被引:76
|
作者
Mostoufi, N
Chaouki, J
机构
[1] Ecole Polytech Montreal, Dept Chem Engn, Montreal, PQ H3C 3A7, Canada
[2] Univ Tehran, Proc Design & Simulat Res Ctr, Dept Chem Engn, Fac Engn, Tehran, Iran
关键词
fluidization; hydrodynamics; multiphase flow; powder technology; cluster; particle tracking;
D O I
10.1016/j.ces.2004.06.006
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
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. (C) 2004 Elsevier Ltd. All rights reserved.
引用
收藏
页码:4217 / 4227
页数:11
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