Reaction coupling in catalytic membrane reactors

被引：20

作者：

Gobina, E

Hughes, R

机构：

[1] Department of Chemical Engineering, University of Salford

来源：

CHEMICAL ENGINEERING SCIENCE | 1996年 / 51卷 / 11期

关键词：

D O I：

10.1016/0009-2509(96)00195-9

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

An experimental and modelling study of the catalytic dehydrogenation of n-butane has been made in a membrane reactor. Use of nitrogen, carbon monoxide/nitrogen and oxygen/nitrogen sweep gases produced conversions up to 5 to 8 times the equilibrium conversion, the largest values occuring due to reaction coupling of the permeated hydrogen with O-2 or CO.

引用

页码：3045 / 3050

页数：6

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