ON ROEL OF TRANSPORT PHENOMENA IN CATALYTIC REACTOR BEHAVIOR DIGITAL SIMULATION OF NAPHTHALENE OXIDATION OVER V205

被引：78

作者：

CARBERRY, JJ

WHITE, D

机构：

来源：

INDUSTRIAL AND ENGINEERING CHEMISTRY | 1969年 / 61卷 / 07期

关键词：

D O I：

10.1021/ie50715a008

中图分类号：

O69 [应用化学];

学科分类号：

081704 ;

摘要：

A steady-state behavior model of a fixed-bed catalytic reactor demonstrates parametric sensitivity and selectivity in naphthalene oxidation. © 1969, American Chemical Society. All rights reserved.

引用

收藏

页码：27 / &

相关论文

共 27 条

[21] Relation between catalytic activity and size of particle
Thiele, EW
[J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1939, 31 : 916 - 920
[22] VONROSENBERG DU, 1962, BRIT CHEM ENG, V7, P186
[23] THE BEHAVIOUR OF POROUS CATALYST PARTICLES IN VIEW OF INTERNAL MASS AND HEAT DIFFUSION EFFECTS
WEISZ, PB
HICKS, JS
[J]. CHEMICAL ENGINEERING SCIENCE, 1962, 17 (04) : 265 - 275
[24] WEISZ PB, 1955, J PHYS CHEM, V59, P423
[25] WENDEL M, 1963, AICHE J, V9, P129
[26] MAXIMUM ALLOWABLE TEMPERATURES IN CHEMICAL REACTORS
WESTERTERP, KR
[J]. CHEMICAL ENGINEERING SCIENCE, 1962, 17 (06) : 423 - 433
[27] HEAT AND MASS TRANSFER FROM WALL TO FLUID IN PACKED BEDS
YAGI, S
WAKAO, N
[J]. AICHE JOURNAL, 1959, 5 (01) : 79 - 85