RESPONSE OF A TUBULAR HETEROGENEOUS CATALYTIC REACTOR TO A STEP INCREASE IN FLOW RATE

被引：19

作者：

LEHR, CG

YURCHAK, S

KABEL, RL

机构：

[1] Pennsylvania State University, University Park, Pennsylvania

[2] Xerox Corporation, Rochester, New York

[3] University of Wisconsin, Madison, Wisconsin

来源：

AICHE JOURNAL | 1968年 / 14卷 / 04期

关键词：

D O I：

10.1002/aic.690140415

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

The vapor phase dehydration of ethanol to diethyl ether, as catalyzed by ion exchange resin, has been studied experimentally and theoretically for the transient state period following a step increase in flow rate. A mathematical model is developed to account quantitatively for the effects of adsorption and surface reaction on the product distribution in the effluent of a tubular reactor. The solution of the model is in good agreement with the experimentally observed behavior. Copyright © 1968 American Institute of Chemical Engineers

引用

页码：627 / &

共 15 条

[1] METHOD OF CHARACTERISTICS TECHNIQUE - APPLICATION TO HEAT AND MASS TRANSFER PROBLEMS [J].