A mechanistic analysis of shell-side two-phase flow in an idealised in-line tube bundle

被引:6
作者
McNeil, David A. [1 ]
Sadikin, Azmahani [1 ]
Bamardouf, Khalid H. [1 ]
机构
[1] Heriot Watt Univ, Dept Mech Engn, Sch Engn & Phys Sci, Edinburgh EH14 4AS, Midlothian, Scotland
关键词
Heat exchanger; Void fraction; Pressure drop; Drift flux; Drag coefficient; Flow pattern; CROSS-FLOW; HYDRODYNAMICS; PATTERN;
D O I
10.1016/j.ijmultiphaseflow.2012.05.004
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
This paper reports on an experimental study of air-water mixtures flowing through an idealised shell and tube, in-line heat exchanger. Void fraction measurements are reported for the minimum gaps between the tubes at near atmospheric conditions. The pressure distributions around some tubes are also reported. These data are combined with data available in the open literature to investigate pressure drop and void fraction prediction methods for these heat exchangers. The data are shown to be flow pattern dependent. Criteria for flow pattern boundaries are deduced from previously published flow maps. Void fraction data in the maximum gap between the tubes are shown to be compatible with the drift flux model and to be different in magnitude to the minimum gap values, which are shown to result from acceleration phenomena in the gaps between the tubes. The pressure drop data are analysed through a one-dimensional model that incorporates separation and re-attachment phenomena. The frictional pressure drop is shown to depend on a liquid layer located on the upper portion of the tubes at low gas velocity and on acceleration effects at high gas velocity. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:53 / 69
页数:17
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