THEORETICAL PATTERNS OF SELECTIVITY IN AGING CATALYSTS WITH SPECIAL REFERENCE TO CATALYTIC CRACKING OF PETROLEUM

被引：31

作者：

CAMPBELL, DR

WOJCIECH.BW

机构：

[1] Department of Chemical Engineering, Queen's University, Kingston, Ontario

来源：

CANADIAN JOURNAL OF CHEMICAL ENGINEERING | 1969年 / 47卷 / 04期

关键词：

D O I：

10.1002/cjce.5450470421

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

The catalyst decay theory of Wojciechowski1 is applied to a simplified theoretical mechanism of catalytic gas oil cracking. The resulting patterns of selectivity are presented and general conclusions drawn. It is shown that selectivity in gas oil cracking is bounded by optimum and minimum performance envelopes which confine the range of possible product distributions. Copyright © 1969 Canadian Society for Chemical Engineering

引用

页码：413 / &

共 5 条

[1] KINETIC DATA AND PRODUCT DISTRIBUTIONS FROM FIXED BED CATALYTIC REACTORS SUBJECT TO CATALYST FOULING [J].

FROMENT, GF ;

BISCHOFF, KB .

CHEMICAL ENGINEERING SCIENCE, 1962, 17 (02) :105-&

[2]

RIEBERT L, 1968, IND ENG CHEM FUNDAME, V7, P125

[3] A MODEL OF CATALYTIC CRACKING CONVERSION IN FIXED MOVING AND FLUID-BED REACTORS [J].

WEEKMAN, VW .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1968, 7 (01) :90-&

[4] REACTION RATES AND SELECTIVITY IN CATALYST PORES [J].

WHEELER, A .

ADVANCES IN CATALYSIS, 1951, 3 :249-327

[5] A THEORETICAL TREATMENT OF CATALYST DECAY [J].

WOJCIECHOWSKI, BW .

CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1968, 46 (01) :48-+

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