CATALYTIC REACTIONS IN TRANSPORT-LINE REACTORS

被引：17

作者：

VARGHESE, P ^{[1
]}

VARMA, A ^{[1
]}

机构：

[1] UNIV NOTRE DAME,DEPT CHEM ENGN,NOTRE DAME,IN 46556

来源：

CHEMICAL ENGINEERING SCIENCE | 1979年 / 34卷 / 03期

关键词：

D O I：

10.1016/0009-2509(79)85065-4

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

The case of an irreversible first order catalytic reaction is considered in a transport-line reactor, via a model which assumes plug flow of both the solid and gas phases, to investigate reactor performance as a function of major operating variables. Under certain fluid mechanical assumptions, a detailed study is made of the effect of catalyst particle size on reactor conversion. © 1979.

引用

页码：337 / 343

页数：7

共 7 条

[1]

Carberry J. J., 1976, CHEM CATALYTIC REACT

[2]

Crank J, 1975, MATH DIFFUSION, V13

[3]

KUNII D, 1969, FLUIDIZATION ENGINEE

[4] CATALYTIC REACTIONS IN TRANSPORT REACTORS [J].