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
相关论文
共 50 条
[21]   HEAT-TRANSFER IN PACKED-BED REACTORS WITH ONE PHASE FLOW [J].
SPECCHIA, V ;
BALDI, G ;
SICARDI, S .
CHEMICAL ENGINEERING COMMUNICATIONS, 1980, 4 (2-3) :361-380
[22]   Microfabricated multiphase packed-bed reactors: Characterization of mass transfer and reactions [J].
Losey, MW ;
Schmidt, MA ;
Jensen, KF .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2001, 40 (12) :2555-2562
[23]   MASS-TRANSFER FOR 2-PHASE COCURRENT DOWNFLOW IN A PACKED-BED [J].
SYLVESTER, ND ;
PITAYAGULSARN, P .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1975, 14 (04) :421-426
[24]   MASS-TRANSFER IN A PACKED-BED OF RASCHIG RINGS AT LOW PECLET NUMBERS [J].
RAO, SP ;
GNIELINSKI, V .
LETTERS IN HEAT AND MASS TRANSFER, 1980, 7 (04) :257-273
[25]   Heat-transfer studies in packed-bed catalytic reactors of low tube/particle diameter ratio [J].
Castillo-Araiza, C. O. ;
Jimenez-Islas, H. ;
Lopez-Isunza, F. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (23) :7426-7435
[26]   HEAT-TRANSFER IN A PACKED-BED [J].
HUGHMARK, GA .
AICHE JOURNAL, 1976, 22 (01) :198-199
[27]   Runaway limits for adiabatic packed-bed catalytic reactors [J].
Christoforatou, EL ;
Balakotaiah, V ;
West, DH .
AICHE JOURNAL, 1998, 44 (02) :394-404
[28]   UNSTEADY, TWO-DIMENSIONAL HEAT AND MASS-TRANSFER IN A PACKED-BED OF FINE PARTICLES WITH AN ENDOTHERMIC PROCESS [J].
HASATANI, M ;
ARAI, N .
CHEMICAL ENGINEERING COMMUNICATIONS, 1981, 10 (4-5) :223-242
[29]   MODELING AND SIMULATION OF HEAT AND MASS-TRANSFER IN A PACKED-BED OF SOLID PARTICLES HAVING HIGH DIFFUSION RESISTANCE [J].
PALANCZ, B .
COMPUTERS & CHEMICAL ENGINEERING, 1985, 9 (06) :567-581
[30]   Numerical analysis of mass transfer in packed-bed reactors with irregular particle arrangements [J].
Atmakidis, Theodoros ;
Kenig, Eugeny Y. .
CHEMICAL ENGINEERING SCIENCE, 2012, 81 :77-83
12345