MTG process in a fixed-bed reactor. Operation and simulation of a pseudoadiabatic experimental unit

被引：16

作者：

Aguayo, AT ^{[1
]}

Gayubo, AG ^{[1
]}

Castilla, M ^{[1
]}

Arandes, JM ^{[1
]}

Olazar, M ^{[1
]}

Bilbao, J ^{[1
]}

机构：

[1] Univ Basque Country, Dept Ingn Quim, E-48080 Bilbao, Spain

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH | 2001年 / 40卷 / 26期

关键词：

D O I：

10.1021/ie0101893

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

A simulation model has been proposed and used to predict the behavior of a laboratory pseudoadiabatic reactor for the transformation of methanol into hydrocarbons. The model incorporates recent advances in the kinetic modeling of the main reaction steps and of the deactivation by coke of the catalyst in the 350-450 degreesC range and is efficient for analyzing the effect of process conditions (space time, water content and inert gas in the feed, and inlet temperature) on the evolution with time on stream of the temperature profile along the reactor and on the yields of the product lumps.

引用

页码：6087 / 6098

页数：12

共 48 条

[1] MODELING OF BUTENE-1 DEHYDROGENATION IN A FIXED-BED REACTOR - BED AND PELLET PROFILES [J].