TRICKLE-BED REACTOR PERFORMANCE .1. HOLDUP AND MASS-TRANSFER EFFECTS

被引:248
作者
GOTO, S [1 ]
SMITH, JM [1 ]
机构
[1] UNIV CALIF,DEPT CHEM ENGN,DAVIS,CA 95616
关键词
D O I
10.1002/aic.690210410
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
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页码:706 / 713
页数:8
相关论文
共 22 条
[1]  
BALDI G, 1974, IND ENG CHEM PROD RD, V13, P447, DOI 10.1021/i260052a026
[2]   EFFECTIVENESS FACTORS FOR GENERAL REACTION RATE FORMS [J].
BISCHOFF, KB .
AICHE JOURNAL, 1965, 11 (02) :351-&
[3]  
EVANS GC, 1953, CHEM ENG PROG, V49, P135
[4]   LIQUID-PHASE DISPERSION IN PACKED BEDS WITH 2-PHASE FLOW [J].
FURZER, IA ;
MICHELL, RW .
AICHE JOURNAL, 1970, 16 (03) :380-&
[5]   OXIDATION OF SO2 IN A TRICKLE-BED REACTOR PACKED WITH CARBON [J].
HARTMAN, M ;
COUGHLIN, RW .
CHEMICAL ENGINEERING SCIENCE, 1972, 27 (05) :867-&
[6]  
Himmelblau D.M., 1960, J CHEM ENG DATA, V5, P10
[7]  
Hoog H., 1953, PETROL REFINER, V32, P137
[8]  
HOUGEN OA, 1947, CHEM PROCESS PRINC 3, P873
[9]   LIQUID-SIDE MASS TRANSFER COEFFICIENTS IN PACKED TOWERS [J].
ONDA, K ;
SADA, E ;
MURASE, Y .
AICHE JOURNAL, 1959, 5 (02) :235-239
[10]  
Otake T, 1953, KAGUKU KOGAKU CHEM E, V17, P176, DOI 10.1252/kakoronbunshu1953.17.176