SIMULTANEOUS HEAT AND MASS-TRANSFER IN PACKED-BED CATALYTIC REACTORS

被引：4
|
作者：
KAMIUTO, K
SAITOH, S
机构：
[1] Department of Production Systems Engineering, Oita University, Oita
来源：
JOURNAL OF THERMOPHYSICS AND HEAT TRANSFER | 1995年 / 9卷 / 03期
关键词：
D O I：
10.2514/3.696
中图分类号：
O414.1 [热力学];
学科分类号：
摘要：
Our previous quasihomogeneous model for heat transfer in packed beds is extended so os to include mass transfer in the beds. A porosity-dependent mass dispersion coefficient is incorporated into the previous model. To examine the adequacy of the model, the sulfer dioxide reactor of Schuler et al. is analyzed theoretically utilizing a finite difference scheme. The theoretical results agreed well with the experimental data without introducing any adjustable parameters.
引用
收藏
页码：524 / 530
页数：7
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