FLOW MICROREACTOR FOR STUDY OF HIGH-PRESSURE CATALYTIC HYDROPROCESSING REACTIONS

被引：31

作者：

ELIEZER, KF ^{[1
]}

BHINDE, M ^{[1
]}

HOUALLA, M ^{[1
]}

BRODERICK, D ^{[1
]}

GATES, BC ^{[1
]}

KATZER, JR ^{[1
]}

OLSON, JH ^{[1
]}

机构：

[1] UNIV DELAWARE,DEPT CHEM ENGN,NEWARK,DE 19711

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS | 1977年 / 16卷 / 03期

关键词：

D O I：

10.1021/i160063a014

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：380 / 384

页数：5

共 12 条

[1]

ANDERSON RB, 1968, EXPT METHODS CATALYT, pCH1

[2]

BHINDE M, 1977, THESIS U DELAWARE

[3]

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[4]

DEBRUIJN A, 1977, 6TH P INT C CAT

[5]

DORAISWAMY LK, 1974, CATAL REV, V10, P177, DOI 10.1080/01614947408079629

[6]

ELIEZER KF, 1976, THESIS U DELAWARE

[7] HYDROCRACKING OF HEAVY PETROLEUM FRACTIONS - PROCESS FLEXIBILITY AND REACTION-MECHANISM [J].

HEDDEN, K ;

WEITKAMP, J .

CHEMIE INGENIEUR TECHNIK, 1975, 47 (12) :505-513

[8] TESTS FOR TRANSPORT LIMITATIONS IN EXPERIMENTAL CATALYTIC REACTORS [J].

MEARS, DE .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1971, 10 (04) :541-&

[9] EFFECT OF HOLDUP INCOMPLETE CATALYST WETTING AND BACKMIXING DURING HYDROPROCESSING IN TRICKLE BED REACTORS [J].

PARASKOS, JA ;

FRAYER, JA ;

SHAH, YT .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1975, 14 (03) :315-322

[10] TRICKLE-BED REACTORS [J].

SATTERFIELD, CN .

AICHE JOURNAL, 1975, 21 (02) :209-228

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