RADIAL PARTICLE MIXING IN GAS SOLIDS FLUIDIZED-BEDS

被引:25
作者
FAN, LT
SONG, JC
YUTANI, N
机构
[1] Kansas State Univ, Dep of Chemical, Engineering, Manhattan, KS, USA, Kansas State Univ, Dep of Chemical Engineering, Manhattan, KS, USA
关键词
CHEMICAL EQUIPMENT - Design - CHEMICAL OPERATIONS - Fluidization;
D O I
10.1016/0009-2509(86)85204-6
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Difficulties involved in experimentally determining the mixing coefficients of particles in a gas-solids fluidized bed are well known. From the theoretical point of view, the mechanism of particle mixing in such a fluidized bed is influenced profoundly by complicated and stochastic phenomena, such as jetting and bubbling. It appears that a sufficiently effective deterministic approach is not available to analyze the mechanism. In the present work, the particle mixing in the radial or lateral direction of a gas-solids fluidized bed was studied by using heated particles as the tracer particles. The transient concentration distribution of these particles in the lateral direction was obtained by means of an impulse response technique; sensitive thermocouples were used for measurement. This work is pertinent to mixing equipment design.
引用
收藏
页码:117 / 122
页数:6
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