PREDICTION OF PACKED-BED CATALYTIC REACTOR PERFORMANCE FOR A COMPLEX-REACTION (OXIDATION OF ORTHO-XYLENE TO PHTHALIC-ANHYDRIDE)

被引：21

作者：

CHANDRASEKHARAN, K

CALDERBANK, PH

机构：

[1] School of Engineering Science, University of Edinburgh, Edinburgh, EH9 3JL Scotland, King's Buildings, Mayfield Road

来源：

CHEMICAL ENGINEERING SCIENCE | 1979年 / 34卷 / 11期

关键词：

D O I：

10.1016/0009-2509(79)80024-X

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

Statistical best-fit kinetic and transport parameters are derived from temperature and yield profiles observed in a pilot-plant catalytic reactor in which o-xylene is oxidised with air to phthalic anhydride and its precursors. Published data are used to begin the search routine and the tuned parameters are seen to be plaubible. The overall model has good extrapolative power to the point where catalyst deactivation becomes apparent. © 1979.

引用

页码：1323 / 1331

页数：9

共 28 条

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