Mass transfer between bubbles and the dense phasein gas fluidized beds

被引:0
|
作者
Hongyong Xie [1 ]
Zhiguo Sun [1 ]
机构
[1] School of Urban Development and Environmental Engineering,Shanghai Second Polytechnic University
关键词
Fluidized beds; Bubbles; Dense phase; Mass transfer; Effective diffusion coefficient;
D O I
暂无
中图分类号
TQ021.4 [扩散、传质过程及原理]; TQ051.13 [];
学科分类号
080706 ; 081701 ; 081704 ;
摘要
Mass transfer between a bubble and the dense phase in gas fluidized beds of Group A and Group B particles was proposed based on previous experimental results and literature data.The mass transfer coefficient between bubbles and the dense phase was determined by k;= 0.21d;.A theoretical analysis of the mass transfer coefficient between a bubble and the dense phase using diffusion equations showed that the mass transfer coefficient between a bubble and the dense phase is k;∝ε;(Du;/d;);in both three- and two-dimensional fluidized beds.An effective diffusion coefficient in gas fluidized beds was introduced and correlated with bubble size as De = 13.3d;7 for Group A and Group B particles.The mass transfer coefficient k;can then be expressed as k;= 0.492ε;(u;d;);for bubbles in a three-dimensional bed and k;= 0.576ε;(u;d;);for bubbles in a two-dimensional bed.
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页码:213 / 217
页数:5
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