A NEW, IMPROVED LIQUID HOLD-UP CORRELATION FOR TRICKLE-BED REACTORS

被引:96
作者
ELLMAN, MJ [1 ]
MIDOUX, N [1 ]
WILD, G [1 ]
LAURENT, A [1 ]
CHARPENTIER, JC [1 ]
机构
[1] ECOLE NATL SUPER IND CHIM,CNRS,SCI GENIE CHIM LAB,1 RUE GRANDVILLE,BP 451,F-54001 NANCY,FRANCE
关键词
D O I
10.1016/0009-2509(90)87046-U
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Presently available liquid hold-up correlations for trickle-bed reactors are not applicable over wide ranges of system conditions. The new, improved correlation for the liquid hold-up in a trickle-bed reactor presented here, derived from fundamental considerations and a wide-ranging data base of some 5000 hydrodynamic experimental results, is applicable to industrial trickle-bed reactors since it is based on wide variations of all the important variables, including measurements at high pressures. No other previously derived correlations are applicable to high pressure operations. A comparison with recent data on liquid hold-up in co-current upflow of gas and liquid shows that the correlation proposed for high interaction downflow gives a fair estimate of the upflow data, as long as the liquid is not foaming. © 1990.
引用
收藏
页码:1677 / 1684
页数:8
相关论文
共 51 条
[1]   RETENTION LEVELS FOR GAS-LIQUID FLOWS WITH DOWN FLOW IN COLUMS WITH IMMERSED AND MOISTENED FILLINGS [J].
BAKOS, M ;
CHARPENT.JC .
CHEMICAL ENGINEERING SCIENCE, 1970, 25 (11) :1822-&
[2]   MODEL FOR MASS-TRANSFER WITH AND WITHOUT CHEMICAL-REACTION IN PACKED TOWERS [J].
BALDI, G ;
SICARDI, S .
CHEMICAL ENGINEERING SCIENCE, 1975, 30 (5-6) :617-624
[3]  
BALDI G, 1981, NATO ADV STUDY I E, V52, P271
[4]   SOME LIQUID HOLDUP EXPERIMENTAL-DATA IN TRICKLE-BED REACTORS FOR FOAMING AND NONFOAMING HYDROCARBONS [J].
CHARPENTIER, JC ;
FAVIER, M .
AICHE JOURNAL, 1975, 21 (06) :1213-1218
[5]   PRESSURE DROP FOR CO-CURRENT FLOW IN WET-PACKED COLUMNS AND COMPARSION WITH BUBBLE COLUMNS [J].
CHARPENTIER, JC ;
PROST, C ;
LEGOFF, P .
CHEMICAL ENGINEERING SCIENCE, 1969, 24 (12) :1777-+
[6]  
CHARPENTIER JC, 1979, CHEM ENG GAS LIQUID
[7]  
CHARPENTIER JC, 1968, THESIS U NANCY NANCY
[8]  
CHARPENTIER JC, 1971, 2ND P C APPL PHYS CH, V2, P31
[9]   DYNAMIC LIQUID HOLDUP IN 2-PHASE DOWNFLOW IN PACKED-BEDS - AIR-SILICONE OIL SYSTEM [J].
CLEMENTS, LD ;
SCHMIDT, PC .
AICHE JOURNAL, 1980, 26 (02) :317-319
[10]   A NEW, IMPROVED PRESSURE-DROP CORRELATION FOR TRICKLE-BED REACTORS [J].
ELLMAN, MJ ;
MIDOUX, N ;
LAURENT, A ;
CHARPENTIER, JC .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (08) :2201-2206