THE DYNAMIC BEHAVIOR OF FLUIDIZED-BED REACTORS FOR SOLID CATALYZED GAS-PHASE OLEFIN POLYMERIZATION

被引：154

作者：

CHOI, KY ^{[1
]}

RAY, WH ^{[1
]}

机构：

[1] UNIV WISCONSIN,DEPT CHEM ENGN,MADISON,WI 53706

来源：

CHEMICAL ENGINEERING SCIENCE | 1985年 / 40卷 / 12期

关键词：

D O I：

10.1016/0009-2509(85)85128-9

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：2261 / 2279

页数：19

共 21 条

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[2]

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AMUNDSON, NR .

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[4] MODELING OF FLUIDIZED-BED REACTORS .2. UNIFORM CATALYST TEMPERATURE AND CONCENTRATION [J].

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AMUNDSON, NR .

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[5] ANALYSIS OF A MODEL FOR A NONISOTHERMAL CONTINUOUS FLUIDIZED-BED CATALYTIC REACTOR [J].

BUKUR, DB ;

WITTMANN, CV ;

AMUNDSON, NR .

CHEMICAL ENGINEERING SCIENCE, 1974, 29 (05) :1173-1192

[6] RECENT DEVELOPMENTS IN TRANSITION-METAL CATALYZED OLEFIN POLYMERIZATION - A SURVEY .2. PROPYLENE POLYMERIZATION [J].

CHOI, KY ;

RAY, WH .

JOURNAL OF MACROMOLECULAR SCIENCE-REVIEWS IN MACROMOLECULAR CHEMISTRY AND PHYSICS, 1985, C25 (01) :57-97

[7]

CHOI KY, 1985, J MACROMOL SCI R M C, VC25, P1

[8]

CHOI KY, 1983, POLYM REACTION ENG, P314

[9]

CHOI KY, 1984, THESIS U WISCONSIN

[10]

CHOI KY, 1982, P IUPAC M AMHERST, P240

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