Mass transfer in axial flows through randomly packed fiber bundles with constant wall concentration

被引:29
作者
Bao, LH [1 ]
Lipscomb, GG [1 ]
机构
[1] Univ Toledo, Dept Chem & Environm Engn, Toledo, OH 43606 USA
基金
美国国家科学基金会;
关键词
Graetz number; fiber packing; mass transfer coefficient; axial flows; finite element-finite difference method;
D O I
10.1016/S0376-7388(02)00043-1
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
An analysis of the effects of fiber packing on shell-side mass transfer coefficients for axial fluid flow through fiber bundles with uniform wall concentration is presented. A combined finite element (FE)-finite difference (FD) method is used to solve the governing conservation of momentum and mass equations. Results are given for values of the Graetz number that range from the entry mass transfer limit to the well-developed limit. Effective mass transfer coefficients for randomly packed fiber bundles can be much lower than for regularly packed fiber bundles for a given fiber packing fraction and Graetz number. Regions of higher fiber packing have lower flow and experience greater mass transfer than regions of lower fiber packing. The changes in the low packing regions dominate, because of the higher flow, and lead to a reduction in the overall mass transfer coefficient. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:207 / 220
页数:14
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