Cryogenic Liquid Slug and Taylor Bubble Length Distributions in an Inclined Tube
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Cryogenic Liquid Slug and Taylor Bubble Length Distributions in an Inclined Tube
Cryogenic Liquid Slug and Taylor Bubble Length Distributions in an Inclined Tube
中国化学工程学报(英文版)2009年17卷第1期 页码:20-26
Affiliations:
Institute of Engineering Thermo-physics, Shanghai Jiao Tong University,Shanghai,China,200240
Author bio:
Funds:
Supported by the National Natural Science Foundation of China (50476015);National High Technology Research and Development Program of China (2006AA09Z333)
王淑华, 张华, 王经. Cryogenic Liquid Slug and Taylor Bubble Length Distributions in an Inclined Tube[J]. 中国化学工程学报(英文版), 2009,17(1):20-26.
WANG Shuhua, ZHANG Hua, WANG Jing. Cryogenic Liquid Slug and Taylor Bubble Length Distributions in an Inclined Tube[J]. , 2009, 17(1): 20-26.
王淑华, 张华, 王经. Cryogenic Liquid Slug and Taylor Bubble Length Distributions in an Inclined Tube[J]. 中国化学工程学报(英文版), 2009,17(1):20-26.DOI: 10.1016/S1004-9541(09)60027-6.
WANG Shuhua, ZHANG Hua, WANG Jing. Cryogenic Liquid Slug and Taylor Bubble Length Distributions in an Inclined Tube[J]. , 2009, 17(1): 20-26.DOI: 10.1016/S1004-9541(09)60027-6.
Cryogenic Liquid Slug and Taylor Bubble Length Distributions in an Inclined Tube
An experimental study was carried out to understand the phenomena of the boiling flow of liquid nitrogen in an inclined tube with closed bottom by using a high speed motion analyzer.The experimental tube is 0.018 m ID and 1.0 m in length.The range of the inclination angle is 45°-90° from the horizontal.The experiment focused on the effect of the inclination angle show that the mean liquid slug length
and Taylor bubble length increase with the increasing
x/D
at various inclination angles.At the same
x/D
the mean liquid slug length and Taylor bubble length increase first
and then decrease with decreasing inclination angles
with the maximum at 60°.In the vertical tube
standard deviation of the nitrogen Taylor bubble length increase with the increasing
x/D
.For the inclined tube
standard deviation of the nitrogen Taylor bubble length increases first
and then decreases with the increasing
x/D
.Standard deviation of the liquid slug length increases with increasing
x/D
for all inclination angles.
Abstract
An experimental study was carried out to understand the phenomena of the boiling flow of liquid nitrogen in an inclined tube with closed bottom by using a high speed motion analyzer.The experimental tube is 0.018 m ID and 1.0 m in length.The range of the inclination angle is 45°-90° from the horizontal.The experiment focused on the effect of the inclination angle show that the mean liquid slug length and Taylor bubble length increase with the increasing
x/D
at various inclination angles.At the same
x/D
the mean liquid slug length and Taylor bubble length increase first
and then decrease with decreasing inclination angles
with the maximum at 60°.In the vertical tube
standard deviation of the nitrogen Taylor bubble length increase with the increasing
x/D
.For the inclined tube
standard deviation of the nitrogen Taylor bubble length increases first
and then decreases with the increasing
x/D
.Standard deviation of the liquid slug length increases with increasing
x/D
for all inclination angles.
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