CATALYST DILUTION FOR IMPROVED PERFORMANCE OF LABORATORY TRICKLE-FLOW REACTORS

被引:83
作者
VANKLINKEN, J
VANDONGEN, RH
机构
关键词
D O I
10.1016/0009-2509(80)80070-4
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
引用
收藏
页码:59 / 66
页数:8
相关论文
共 16 条
[1]  
DEBRUIJN A, 1976, 6TH INT C CAT LOND
[2]   SCALE UP OF PILOT-PLANT DATA FOR CATALYTIC HYDROPROCESSING [J].
HENRY, HC ;
GILBERT, JB .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1973, 12 (03) :328-334
[3]   2-PHASE COCURRENT DOWNFLOW IN PACKED BEDS [J].
HOCHMAN, JM ;
EFFRON, E .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1969, 8 (01) :63-&
[4]  
KOROS RM, 1976, 4TH INT S REACT ENG
[5]  
LEVENSPIEL O, 1972, CHEM REACTION ENG, pCH9
[6]  
Mears D. E., 1974, ADV CHEM SER, V133, P218
[7]   ROLE OF AXIAL DISPERSION IN TRICKLE-FLOW LABORATORY REACTORS [J].
MEARS, DE .
CHEMICAL ENGINEERING SCIENCE, 1971, 26 (09) :1361-&
[8]   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
[9]   2-PHASE FLOW IN PACKED BEDS - EVALUATION OF AXIAL DISPERSION AND HOLDUP BY MOMENT ANALYSIS [J].
SATER, VE ;
LEVENSPI.O .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1966, 5 (01) :86-&
[10]   TRICKLE-BED REACTORS [J].
SATTERFIELD, CN .
AICHE JOURNAL, 1975, 21 (02) :209-228