Flow boiling heat transfer of R134a in the multiport minichannel heat exchangers

被引:66
|
作者
Kaew-On, Jatuporn [1 ,2 ]
Sakamatapan, Kittipong [1 ]
Wongwises, Somchai [1 ]
机构
[1] King Mongkuts Univ Technol Thonburi, Dept Mech Engn, Fluid Mech Thermal Engn & Multiphase Flow Res Lab, Bangkok 10140, Thailand
[2] King Mongkuts Univ Technol Thonburi, Joint Grad Sch Energy & Environm, Bangkok 10140, Thailand
关键词
Flow boiling heat transfer; Multiport minichannels; Tube-in-tube heat exchangers; LMTD; R134a; PRESSURE-DROP; TUBE; DIAMETER; R-134A; PERFORMANCE; WATER; FLUX; CO2;
D O I
10.1016/j.expthermflusci.2010.10.007
中图分类号
O414.1 [热力学];
学科分类号
摘要
The flow boiling heat transfer characteristics of R134a in the multiport minichannel heat exchangers are presented. The heat exchanger was designed as the counter flow tube-in-tube heat exchanger with refrigerant flowing in the inner tube and hot water in the gap between the outer and inner tubes. Two inner tubes were made from extruded multiport aluminium with the internal hydraulic diameter of 1.1 mm for 14 numbers of channels and 1.2 mm for eight numbers of channels. The outer surface areas of two inner test sections are 5979 mm(2) and 6171 m(2), while the inner surface areas are 13,545 mm(2) and 8856 mm(2) for 14 and eight numbers of channels, respectively. The outer tube of heat exchanger was made from circular acrylic tube with an internal hydraulic diameter of 25.4 mm. The experiments were performed at the heat fluxes between 15 and 65 kW/m(2), mass flux of refrigerant between 300 and 800 kg/m(2) s and saturation pressure ranging from 4 to 6 bar. For instance the boiling curve, average heat transfer coefficients are discussed. The comparison results of two test sections with different the number of channels are investigated. The results are also compared with nine existing correlations. The new correlation for predicting the heat transfer coefficient was also proposed. (C) 2010 Elsevier Inc. All rights reserved.
引用
收藏
页码:364 / 374
页数:11
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