SCALE UP OF PILOT-PLANT DATA FOR CATALYTIC HYDROPROCESSING

被引:75
作者
HENRY, HC [1 ]
GILBERT, JB [1 ]
机构
[1] IMPERIAL OIL ENTERPRISES LTD,RES DEPT,SARNIA N7T 7M1,ONTARIO,CANADA
来源
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT | 1973年 / 12卷 / 03期
关键词
D O I
10.1021/i260047a019
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
引用
收藏
页码:328 / 334
页数:7
相关论文
共 19 条
[1]  
BONDI A, 1971, CHEM TECHNOL, P185
[2]  
CECIL RR, 1968, 61 ANN M AICHE LOS A
[3]  
DAVIDSON JF, 1959, T I CHEM ENGRS, V37, P131
[4]  
FLINN RA, 1963, HYDROCARBON P PETROL, V42, P129
[5]  
GILBERT JB, 1965, P AM PETROL I, V45, P29
[6]   2-PHASE COCURRENT DOWNFLOW IN PACKED BEDS [J].
HOCHMAN, JM ;
EFFRON, E .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1969, 8 (01) :63-&
[7]  
LENOBEL JW, 1960, 5 P WORLD PETR C, P233
[8]   ROLE OF AXIAL DISPERSION IN TRICKLE-FLOW LABORATORY REACTORS [J].
MEARS, DE .
CHEMICAL ENGINEERING SCIENCE, 1971, 26 (09) :1361-&
[9]   TESTS FOR TRANSPORT LIMITATIONS IN EXPERIMENTAL CATALYTIC REACTORS [J].
MEARS, DE .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1971, 10 (04) :541-&
[10]   PREDICTION OF LIQUID PHASE HOLD-UP IN RANDOM PACKED BEDS [J].
MOHUNTA, DM ;
LADDHA, GS .
CHEMICAL ENGINEERING SCIENCE, 1965, 20 (12) :1069-&