Two-phase flow patterns in large diameter vertical pipes

被引:17
|
作者
Ali, Shazia F. [1 ]
Yeung, Hoi [2 ]
机构
[1] NED Univ Engn & Technol, Fac Chem & Proc Engn, Karachi 75270, Pakistan
[2] Cranfield Univ, Dept Offshore Proc & Energy Engn, Cranfield MK43 0AL, Beds, England
关键词
vertical flow; large diameter; two-phase flow; flow patterns; flow pattern transitions; GAS-LIQUID FLOW; SLUG TRANSITION; IDENTIFICATION; MODEL; COLUMNS; REGIMES;
D O I
10.1002/apj.1750
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
An experimental investigation of adiabatic upward co-current air-water two-phase flow has been carried out to determine the flow patterns in a 12.2=m-high and 250=mm nominal diameter vertical pipe. The visual observations of flow patterns were supplemented by statistical analysis of the time-averaged void fraction determined by pressure drop method. Four flow patterns were identified in the vertical test section, namely dispersed bubbly, bubbly, agitated bubblyand churn/forth flow within the experimental superficial velocity range ( j(a) = 0.18-2.2 m/s and j(w) = 0.18-1.2 m/s). Conventional slug flow consisting of smooth bullet-shaped bubbles (Taylor bubble) and liquid slugs was never observed; instead, agitated bubbly flow was the most dominant flow pattern in relevant superficial velocity range. On the basis of the visual and statistically extracted information, a flow pattern map was developed and compared with the existing flow pattern maps. Available flow regime transition models compared against the present experimental data yielded poor agreement with none of the existing models predicting the transitions as a whole. A satisfactory agreement was obtained with other large diameter studies with inconsistencies mainly attributable to confusion in the identification of the flow patterns. (c) 2013 Curtin University of Technology and John Wiley & Sons, Ltd.
引用
收藏
页码:105 / 116
页数:12
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