CONTROL OF TRANSPORT-PROPERTIES WITH A MICROPOROUS MEMBRANE REACTOR TO ENHANCE YIELDS IN DEHYDROGENATION REACTIONS

被引：59

作者：

CASANAVE, D

GIROIRFENDLER, A

SANCHEZ, J

LOUTATY, R

DALMON, JA

机构：

[1] INST RECH CATALYSE,CNRS,URA 5401,F-69626 VILLEURBANNE,FRANCE

[2] UNIV LYON 1,AUTOMAT & GENIE PROCEDES LAB,CNRS,URA 1328,F-69622 VILLEURBANNE,FRANCE

[3] CTR RECH TOTAL RAFFINAGE DISTRIBUT,F-76700 HARFLEUR,FRANCE

来源：

CATALYSIS TODAY | 1995年 / 25卷 / 3-4期

关键词：

D O I：

10.1016/0920-5861(95)00129-4

中图分类号：

O69 [应用化学];

学科分类号：

081704 ;

摘要：

The dehydrogenation of isobutane has been studied in a membrane reactor using either a mesoporous alumina membrane or a microporous zeolite membrane. Tt has been shown that for both membranes an increase in the isobutene yield is observed when compared to a conventional reactor. However, these increases are related to two different phenomena: a complete mixing of reactants, products and sweep gas in the case of the mesoporous membrane and a continuous separation of hydrogen when the microporous zeolite membrane was used.

引用

页码：309 / 314

页数：6

共 18 条

[1] CATALYSIS WITH PERMSELECTIVE INORGANIC MEMBRANES [J].