SCI和EI收录∣中国化工学会会刊

›› 2009, Vol. 17 ›› Issue (1): 20-26.

• FLUID FLOW AND TRANSPORT PHENOMENA • Previous Articles     Next Articles

Cryogenic Liquid Slug and Taylor Bubble Length Distributions in an Inclined Tube

WANG Shuhua, ZHANG Hua, WANG Jing   

  1. Institute of Engineering Thermo-physics, Shanghai Jiao Tong University, Shanghai 200240, China
  • Received:2008-06-12 Revised:2008-09-22 Online:2009-01-28 Published:2009-01-28
  • Supported by:
    Supported by the National Natural Science Foundation of China(50476015);National High Technology Research and Development Program of China (2006AA09Z333)

Cryogenic Liquid Slug and Taylor Bubble Length Distributions in an Inclined Tube

王淑华, 张华, 王经   

  1. Institute of Engineering Thermo-physics, Shanghai Jiao Tong University, Shanghai 200240, China
  • 通讯作者: WANG Shuhua, E-mail: shhwang@sjtu.edu.cn
  • 基金资助:
    Supported by the National Natural Science Foundation of China(50476015);National High Technology Research and Development Program of China (2006AA09Z333)

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.

Key words: nitrogen, boiling, Taylor bubble, liquid slug, length distribution, inclined tube

摘要: 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.

关键词: nitrogen, boiling, Taylor bubble, liquid slug, length distribution, inclined tube