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

页码：524 / 530

页数：7

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