EFFECT OF CATALYST PARTICLE-SIZE ON PERFORMANCE OF A TRICKLE-BED REACTOR

被引：3
作者：
MARANGOZIS, J
机构：
来源：
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT | 1980年 / 19卷 / 02期
关键词：
D O I：
10.1021/i260074a023
中图分类号：
TQ [化学工业];
学科分类号：
0817 ;
摘要：
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页码：326 / 328
页数：3
相关论文
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[1]  
MARANGOZIS J, 1980, IND ENG CHEM PROCESS
[2]  
MEARS DE, 1974, ADV CHEM SER, P218
[3]   EFFECT OF CATALYST PARTICLE-SIZE ON PERFORMANCE OF A TRICKLE-BED REACTOR [J].
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PARASKOS, JA .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1977, 16 (01) :152-155
[4]   ROLE OF LIQUID HOLDUP, EFFECTIVE CATALYST WETTING, AND BACKMIXING ON PERFORMANCE OF A TRICKLE BED REACTOR FOR RESIDUE HYDRODESULFURIZATION [J].
MONTAGNA, AA ;
SHAH, YT .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1975, 14 (04) :479-483
[5]   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
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