Effects of equipment dimensions on liquid mixing time of bubble column with draft tube

被引:12
作者
Bando, Y [1 ]
Hayakawa, H
Nishimura, M
机构
[1] Nagoya Univ, Dept Chem Engn, Nagoya, Aichi 4648603, Japan
[2] Gifu Univ, Dept Appl Chem, Gifu 5011112, Japan
关键词
chemical reactor; bubble column; airlift; draft tube; liquid mixing time;
D O I
10.1252/jcej.31.765
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The liquid mixing time of a bubble column with a draft tube is experimentally studied. The diameter and height of the column, the diameter and length of the draft tube, and the mode of sparging gas were changed and the liquid mixing time was measured. The lengths of bottom and top clearances have significant effects on the liquid mixing time. The liquid mixing time increases with increasing column aspect ratio of height to diameter, The liquid mixing time of the bubble column with a draft tube is longer than that of a standard bubble column when the column aspect ratio is relatively high. The liquid mixing time has a minimum when the diameter ratio of draft tube to column is 0.5 to 0.6, These effects of equipment dimensions are expressed by an equation. In the experiment using different solutions, the liquid mixing time becomes shorter with increasing liquid surface tension, or with increasing liquid viscosity.
引用
收藏
页码:765 / 770
页数:6
相关论文
共 13 条
[1]  
BELLO RA, 1984, CAN J CHEM ENG, V62, P573, DOI DOI 10.1002/CJCE.5450620501
[2]   LIQUID CIRCULATION IN AIRLIFT REACTORS [J].
CHISTI, MY ;
HALARD, B ;
MOOYOUNG, M .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (03) :451-457
[3]   TRACER DISPERSION IN A LABORATORY AIR-LIFT REACTOR [J].
FIELDS, PR ;
SLATER, NKH .
CHEMICAL ENGINEERING SCIENCE, 1983, 38 (04) :647-653
[4]   LIQUID CIRCULATION IN A DRAFT-TUBE BUBBLE COLUMN [J].
JONES, AG .
CHEMICAL ENGINEERING SCIENCE, 1985, 40 (03) :449-462
[5]  
KAWASE Y, 1986, J CHEM TECHNOL BIOT, V36, P527
[6]   LIQUID-PHASE MIXING IN BUBBLE-COLUMNS WITH NEWTONIAN AND NON-NEWTONIAN FLUIDS [J].
KAWASE, Y ;
MOOYOUNG, M .
CHEMICAL ENGINEERING SCIENCE, 1986, 41 (08) :1969-1977
[7]   LIQUID CIRCULATION, GAS HOLDUP AND PRESSURE-DROP IN BUBBLE COLUMN WITH DRAFT TUBE [J].
KOIDE, K ;
IWAMOTO, S ;
TAKASAKA, Y ;
MATSUURA, S ;
TAKAHASHI, E ;
KIMURA, M ;
KUBOTA, H .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1984, 17 (06) :611-618
[8]   GAS HOLDUP AND VOLUMETRIC LIQUID-PHASE MASS-TRANSFER COEFFICIENT IN BUBBLE COLUMN WITH DRAFT TUBE AND WITH GAS DISPERSION INTO ANNULUS [J].
KOIDE, K ;
SATO, H ;
IWAMOTO, S .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1983, 16 (05) :407-413
[9]   GAS HOLDUP AND VOLUMETRIC LIQUID-PHASE MASS-TRANSFER COEFFICIENT IN BUBBLE COLUMN WITH DRAFT TUBE AND WITH GAS DISPERSION INTO TUBE [J].
KOIDE, K ;
KUREMATSU, K ;
IWAMOTO, S ;
IWATA, Y ;
HORIBE, K .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1983, 16 (05) :413-419
[10]   CONTRIBUTIONS OF ANNULUS AND DRAFT TUBE TO GAS-LIQUID MASS-TRANSFER IN BUBBLE-COLUMNS WITH DRAFT TUBE [J].
KOIDE, K ;
HORIBE, K ;
KITAGUCHI, H ;
SUZUKI, N .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1984, 17 (05) :547-549