Flow boiling pressure drop of R134a in the counter flow multiport minichannel heat exchangers

被引:19
作者
Kaew-On, Jatuporn [1 ,2 ]
Sakamatapan, Kittipong [1 ]
Wongwises, Somchai [1 ,3 ]
机构
[1] King Mongkuts Univ Technol Thonburi, Fluid Mech Thermal Engn & Multiphase Flow Res Lab, Dept Mech Engn, Bangkok 10140, Thailand
[2] King Mongkuts Univ Technol Thonburi, JGSEE, Bangkok 10140, Thailand
[3] Acad Sci, Royal Inst Thailand, Bangkok 10300, Thailand
关键词
Flow boiling pressure drop; Multiport minichannels; Tube-in-tube heat exchanger; R134a; 2-PHASE FLOW; HORIZONTAL TUBES; PREDICTION; FRICTION; PATTERN; REFRIGERANTS;
D O I
10.1016/j.expthermflusci.2011.09.002
中图分类号
O414.1 [热力学];
学科分类号
摘要
In the present study, the pressure drop characteristics during the boiling of R134a as it flows through the multiport minichannel heat exchangers are presented. The heat exchangers are counter flow tube-in-tubes. The refrigerant flow runs through the inner tube, while the hot water flows through the 25.4 mm round tube at outer edge of the heat exchanger. Two inner test sections are made from aluminium tubing with hydraulic diameters of 1.1 mm for 14 channels and 1.2 mm for eight channels. The experiments were carried out at mass fluxes ranging from 350 to 980 kg/(m(2) s), heat fluxes ranging from 18 to 80 kW/m(2), and saturation pressures of 4, 5 and 6 bar, at constant inlet quality of 0.05. The effect of relevant parameters on the frictional pressure drop, such as the saturation pressure, mass flux, heat flux, and aspect ratio, are examined and discussed in detail. Finally, the nine existing correlations that are based on both conventional tubes and small tubes are selected for comparison with the experimental results. (C) 2011 Elsevier Inc. All rights reserved.
引用
收藏
页码:107 / 117
页数:11
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