EVALUATION PROCEDURE FOR CRACKING CATALYSTS

被引：8

作者：

GUSTAFSON, WR

机构：

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT | 1972年 / 11卷 / 04期

关键词：

D O I：

10.1021/i260044a009

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：507 / +

页数：1

共 12 条

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BLANDING, FH .

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[2] NON-STEADY STATE BEHAVIOUR OF FIXED BED CATALYTIC REACTORS DUE TO CATALYST FOULING [J].

FROMENT, GF ;

BISCHOFF, KB .

CHEMICAL ENGINEERING SCIENCE, 1961, 16 (3-4) :189-201

[3]

GUSTAFSON WR, 1969, ACS DIV PETROL CHEM, V14, pB56

[4]

HENDERSON DS, 1967, OIL GAS J, V65, P88

[5] APPLICATION OF A KINETIC MODEL FOR CATALYTIC CRACKING - EFFECTS OF CHARGE STOCKS [J].

NACE, DM ;

VOLTZ, SE ;

WEEKMAN, VW .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1971, 10 (04) :530-&

[6] CATALYTIC CRACKING OVER CRYSTALLINE ALUMINOSILICATES .I. INSTANTANEOUS RATE MEASUREMENTS FOR HEXADECANE CRACKING [J].

NACE, DM .

INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT, 1969, 8 (01) :24-&

[7]

OZAWA Y, 1968, IND ENG CHEM PROC DD, V7, P72, DOI 10.1021/i260025a015

[8] A MODEL FOULING REACTION IN A ZEOLITE CATALYST [J].

TAN, CH ;

FULLER, OM .

CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1970, 48 (02) :174-&

[9] KINETICS OF CATALYTIC CRACKING SELECTIVITY IN FIXED, MOVING, AND FLUID BED REACTORS [J].

WEEKMAN, VW ;

NACE, DM .

AICHE JOURNAL, 1970, 16 (03) :397-&

[10] 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-&

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