Modelling and simulation of flow maldistribution in random packed columns with gas-liquid countercurrent flow

被引:37
作者
Sun, CG [1 ]
Yin, FH [1 ]
Afacan, A [1 ]
Nandakumar, K [1 ]
Chuang, KT [1 ]
机构
[1] Univ Alberta, Dept Chem & Mat Engn, Edmonton, AB T6G 2G6, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
packed columns; random packings; maldistribution; hydrodynamics; two-phase flow;
D O I
10.1205/026387600527275
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
macroscopic model, based on the volume-averaged equations of momentum and continuity, is presented to predict hydrodynamic characteristics of gas and liquid countercurrent flow in random packed columns. The main advantage of this approach is that the model equations derived from the mass and momentum conversation laws will remain valid on a wider range of length scale, from laboratory to industrial size packed columns. Therefore they can be used as basic tool for more rigorous design and scale up of packed columns. In this study, the large-scale liquid maldistribution was simulated using the proposed model for a 0.6-m diameter column packed with 25 min stainless steel Pall rings. The development of liquid flow patterns along the packed height was obtained for several different initial distributions of liquid phase. Furthermore, the effect of liquid and gas loads on the liquid distribution was examined. The simulation results are in good agreement with the experimental data obtained in our laboratory for both water/air and isopar/air systems.
引用
收藏
页码:378 / 388
页数:11
相关论文
共 35 条
[1]  
ALBRIGHT MA, 1984, HYDROCARB PROCESS, V9, P173
[2]  
Baker T, 1935, T AM INST CHEM ENG, V31, P296
[3]   INFLUENCE OF BED SIZE ON FLOW CHARACTERISTICS AND POROSITY OF RANDOMLY PACKED-BEDS OF SPHERES [J].
BEAVERS, GS ;
SPARROW, EM ;
RODENZ, DE .
JOURNAL OF APPLIED MECHANICS-TRANSACTIONS OF THE ASME, 1973, 40 (03) :655-660
[4]   RADIAL LIQUID SPREAD AND MALDISTRIBUTION IN PACKED-COLUMNS UNDER DIFFERENT WETTING CONDITIONS [J].
BEMER, GG ;
ZUIDERWEG, FJ .
CHEMICAL ENGINEERING SCIENCE, 1978, 33 (12) :1637-1643
[5]   VOID FRACTION DISTRIBUTION IN BEDS OF SPHERES [J].
BENENATI, RF ;
BROSILOW, CB .
AICHE JOURNAL, 1962, 8 (03) :359-361
[6]  
Billet R, 1995, Packed towers in processing and environmental technology
[7]   A STUDY OF THE FLOW OF LIQUID WHEN FREELY TRICKLING OVER THE PACKING IN A CYLINDRICAL TOWER [J].
CIHLA, Z ;
SCHMIDT, O .
COLLECTION OF CZECHOSLOVAK CHEMICAL COMMUNICATIONS, 1957, 22 (03) :896-907
[8]   CORRELATIONS FOR WALL AND PARTICLE-SHAPE EFFECTS ON FIXED-BED BULK VOIDAGE [J].
DIXON, AG .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1988, 66 (05) :705-708
[9]   LIQUID DISTRIBUTION IN PACKED COLUMNS [J].
DUTKAI, E ;
RUCKENSTEIN, E .
CHEMICAL ENGINEERING SCIENCE, 1968, 23 (11) :1365-+
[10]  
ERGUN S, 1952, CHEM ENG PROG, V48, P89