GAS-PHASE DISPERSION IN BUBBLE-COLUMNS

被引:34
作者
WACHI, S [1 ]
NOJIMA, Y [1 ]
机构
[1] KANEGAFUCHI CHEM IND CO LTD,ENGN RES LAB,HYOGO 676,JAPAN
关键词
D O I
10.1016/0009-2509(90)85012-3
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Gas-phase dispersion in bubble columns of 0.5 and 0.2 m diameter was investigated experimentally by the impulse response method at superficial gas velocities in the range 0.029-0.456 m/s. Based on the recirculation theory of bubble columns, the expression for the axial dispersion coefficient of the gas phase was found to be EG = (180/α) UGD 3 2T. The experimental results in water bubble columns were quantitatively described by this equation with the proportional constant α = 9. At gas velocities higher than 0.1 m/s, the gas-phase dispersion was suppressed by the insertion of perforated plates with a free area of 44%. © 1990.
引用
收藏
页码:901 / 905
页数:5
相关论文
共 16 条
[1]   SOME PROPERTIES OF A PACKED BUBBLE COLUMN [J].
CARLETON, AJ ;
FLAIN, RJ ;
RENNIE, J ;
VALENTIN, FH .
CHEMICAL ENGINEERING SCIENCE, 1967, 22 (12) :1839-&
[2]   NON-ISOBARIC BUBBLE-COLUMNS WITH VARIABLE GAS VELOCITY [J].
DECKWER, WD .
CHEMICAL ENGINEERING SCIENCE, 1976, 31 (04) :309-317
[3]  
FIELD RW, 1980, T I CHEM ENG-LOND, V58, P228
[4]  
HILLS JH, 1974, T I CHEM ENG-LOND, V52, P1
[5]  
KUBO K, 1970, KAGAKU KOKAGU, V34, P856
[6]  
Levenspiel O, 1999, CHEM REACTION ENG, Vthird
[7]  
Mangartz K.-H., 1980, VERFAHRENSTECHNIK MA, V14, P40
[8]  
MANGERTZ KH, 1981, CHEM ENG SCI, V31, P1069
[9]  
Miyauchi T., 1970, KAGAKU KOGAKU, V34, pa1
[10]  
Miyauchi T., 1981, ADV CHEM ENG, V11, P275