MODELLING OF CHEMICAL REACTORS .13. NONSTATIONARY HEAT AND MASS TRANSFER IN A PARTICLE OF POROUS CATALYST ONE DIMENSIONAL APPROXIMATION OF MODEL

被引：6

作者：

HLAVACEK, V

MAREK, M

KUBICEK, M

机构：

来源：

关键词：

D O I：

10.1135/cccc19702124

中图分类号：

O6 [化学];

学科分类号：

0703 ;

摘要：

引用

页码：2124 / &

共 14 条

[1] AMUNDSON NR, 1958, CHEM ENG SCI, V7, P121
[2] AMUNDSON R, 1965, AICHE J, V11, P339
[3] CARSLAV HS, 1947, CONDUCTION HEAT SOLI
[4] COBERLY CA, 1951, CHEM ENG PROG, V47, P141
[5] MODELLING OF CHEMICAL REACTORS .I. TUBULAR NON-ISOTHERMAL NON-ADIABATIC PACKED BED REACTOR DESIGN EQUATIONS AND NUMERICAL METHODS
HLAVACEK, V
MAREK, M
[J]. COLLECTION OF CZECHOSLOVAK CHEMICAL COMMUNICATIONS, 1967, 32 (09) : 3291 - &
[6] HLAVACEK V, 1969, COLLECT CZECH CHEM C, V34, P3664
[7] ON STABILITY OF A DETAILED PACKED-BED REACTOR
MCGUIRE, ML
LAPIDUS, L
[J]. AICHE JOURNAL, 1965, 11 (01) : 85 - &
[8] MIRORSKI N, 1962, NONLINEAR OSCILLATIO
[9] PISMEN LM, 1966, DOKL AKAD NAUK SSSR, V168, P266
[10] STABILITY OF A REACTION WITH INTRA-PARTICLE DIFFUSION OF MASS AND HEAT - LIAPUNOV METHODS IN A METRIC FUNCTION SPACE
WEI, J
[J]. CHEMICAL ENGINEERING SCIENCE, 1965, 20 (08) : 729 - &