GAS-LIQUID MASS-TRANSFER IN TAYLOR FLOW THROUGH A CAPILLARY

被引：73

作者：

IRANDOUST, S ^{[1
]}

ERTLE, S ^{[1
]}

ANDERSSON, B ^{[1
]}

机构：

[1] CHALMERS UNIV TECHNOL,DEPT CHEM REACT ENGN,S-41296 GOTHENBURG,SWEDEN

来源：

CANADIAN JOURNAL OF CHEMICAL ENGINEERING | 1992年 / 70卷 / 01期

关键词：

TAYLOR FLOW; SEGMENTED FLOW; MASS TRANSFER; MONOLITH;

D O I：

10.1002/cjce.5450700116

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

The gas-liquid mass transfer in two-phase flow through a capillary has been measured for water air, ethanol-air and ethylene glycol air systems. A semi-theoretical model has been developed and compared with experimental results, and a full computer simulations of the flow pattern and mass transfer using a flow simulation program have been made. The measured values are about 30% less than the calculated values.

引用

页码：115 / 119

页数：5

共 22 条

[1] Bird R B., 2007, TRANSPORT PHENOMENA
[2] Clift R., 1978, BUBBLES DROPS PARTIC
[3] Crank J., 1979, MATH DIFFUSION, V2nd
[4] EDVINSSON R, 1992, IN PRESS
[5] SOLID-LIQUID MASS-TRANSFER IN SEGMENTED GAS-LIQUID FLOW THROUGH A CAPILLARY
HATZIANTONIOU, V
ANDERSSON, B
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1982, 21 (04): : 451 - 456
[6] Infante Ferreira CA, 1985, INT J REFRIG, V8, P326, DOI DOI 10.1016/0140-7007(85)90027-1
[7] SIMULATION OF FLOW AND MASS-TRANSFER IN TAYLOR FLOW THROUGH A CAPILLARY
IRANDOUST, S
ANDERSSON, B
[J]. COMPUTERS & CHEMICAL ENGINEERING, 1989, 13 (4-5) : 519 - 526
[8] SCALING UP OF A MONOLITHIC CATALYST REACTOR WITH 2-PHASE FLOW
IRANDOUST, S
ANDERSSON, B
BENGTSSON, E
SIVERSTROM, M
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1989, 28 (10) : 1489 - 1493
[9] LIQUID-FILM IN TAYLOR FLOW THROUGH A CAPILLARY
IRANDOUST, S
ANDERSSON, B
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1989, 28 (11) : 1684 - 1688
[10] MASS-TRANSFER AND LIQUID-PHASE REACTIONS IN A SEGMENTED 2-PHASE FLOW MONOLITHIC CATALYST REACTOR
IRANDOUST, S
ANDERSSON, B
[J]. CHEMICAL ENGINEERING SCIENCE, 1988, 43 (08) : 1983 - 1988

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