The effect of tube diameter on vertical two-phase flow regimes in small tubes

被引:161
|
作者
Chen, L.
Tian, Y. S.
Karayiannis, T. G. [1 ]
机构
[1] Brunel Univ, Sch Engn & Design, Uxbridge UB8 3PH, Middx, England
[2] Aspentech Inc, Abingdon OX14 4RY, Oxon, England
关键词
flow patterns; two-phase flow; small diameter; vertical;
D O I
10.1016/j.ijheatmasstransfer.2006.03.025
中图分类号
O414.1 [热力学];
学科分类号
摘要
Flow boiling flow patterns in four circular tubes with internal diameters of 1.10, 2.01, 2.88 and 4.26 mm were investigated in the present project. The experiments were conducted in vertical upward two-phase flow using R134a as the working fluid. The observed flow patterns include dispersed bubble, bubbly, confined bubble, slug, churn, annular and mist flow. The flow characteristics in the 2.88 and 4.26 mm, tubes are similar to those typically described in normal size tubes. The smaller diameter tubes, 1.10 and 2.01 mm, exhibit strong "small tube characteristics" as described in earlier studies. The sketched flow maps show that the transition boundaries of slug-churn and churn-annular depend strongly on diameter. On the contrary, the dispersed bubble to churn and bubbly to slug boundaries are less affected. The transition boundaries are compared with existing models for normal size tubes showing poor agreement. (c) 2006 Elsevier Ltd. All rights reserved.
引用
收藏
页码:4220 / 4230
页数:11
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