EFFECT OF CATALYST PORE AND PELLET SIZES ON DEACTIVATION IN SRC OIL HYDROTREATMENT

被引：10

作者：

CHANG, HJ ^{[1
]}

CRYNES, BL ^{[1
]}

机构：

[1] OKLAHOMA STATE UNIV,SCH CHEM ENGN,STILLWATER,OK 74078

来源：

AICHE JOURNAL | 1986年 / 32卷 / 02期

关键词：

D O I：

10.1002/aic.690320208

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：224 / 232

页数：9

共 15 条

[1]

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[2]

CHANG HJ, 1982, THESIS OKLAHOMA STAT

[3]

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[4]

DAUTZENBERG FM, 1978, ACS SYM SER, V65, P254

[5]

HAYNES HW, 1983, CHEM ENG COMMUN, V23, P161, DOI 10.1080/00986448308940472

[6]

LEE JW, 1973, CHEM ENG, V6, P111

[7]

MASAMUNE S, 1966, AICHE J, V12

[8] EFFECT OF INTRAPARATICLE DIFFUSION ON CATALYST FOULING [J].

MURAKAMI, Y ;

KOBAYASH.T ;

HATTORI, T ;

MASUDA, M .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1968, 7 (04) :599-&

[9] CATALYST DEACTIVATION DUE TO PORE-PLUGGING BY REACTION-PRODUCTS [J].

NEWSON, E .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1975, 14 (01) :27-33

[10] USE OF FUNDAMENTAL-CONCEPTS IN CATALYST AGING TO INCREASE CATALYST UTILIZATION DURING COAL-LIQUEFACTION, STEAM REFORMING, AND OTHER CARBON-FORMING REACTIONS [J].

POLINSKI, LM ;

STIEGEL, GJ ;

SAROFF, L .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1981, 20 (03) :470-475

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