Multiple steady states in a reactive distillation column for the production of the fuel ether TAME part II: Experimental validation

被引：0

作者：

Rapmund, P ^{[1
]}

Sundmacher, K ^{[1
]}

Hoffmann, U ^{[1
]}

机构：

[1] Tech Univ Clausthal, Inst Chem Verfahrenstech, D-38678 Clausthal Zellerfeld, Germany

来源：

CHEMICAL ENGINEERING & TECHNOLOGY | 1998年 / 21卷 / 02期

关键词：

D O I：

10.1002/(SICI)1521-4125(199802)21:2<136::AID-CEAT136>3.0.CO;2-4

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

On the market, production technologies for the fuel ether TAME with and without an integrated reaction-separation unit (reactive distillation) are competing. To achieve high conversion of olefins, in most of the processes, a reactive distillation column is incorporated in addition to a standard liquid phase fixed bed reactor.

引用

页码：136 / +

页数：5

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