Thermo-chemical characteristics of R134a flow boiling in helically coiled tubes at low mass flux and low pressure

被引:36
作者
Chen, Chang-Nian [1 ]
Han, Ji-Tian [1 ]
Jen, Tien-Chien [2 ]
Shao, Li [1 ]
机构
[1] Shandong Univ, Sch Energy & Power Engn, Jinan 250061, Shandong, Peoples R China
[2] Univ Wisconsin, Dept Mech Engn, Milwaukee, WI 53201 USA
基金
中国国家自然科学基金;
关键词
Boiling heat transfer; Helically coiled tubes; R134a; Low mass flux and low pressure; CONDENSATION HEAT-TRANSFER; 2-PHASE FLOW; TRANSFER COEFFICIENTS; DROP CHARACTERISTICS; SMOOTH TUBE; HFC-134A; EVAPORATION; R-134A; PATTERN; PIPES;
D O I
10.1016/j.tca.2010.09.020
中图分类号
O414.1 [热力学];
学科分类号
摘要
The characteristics of R134a heat transfer coefficients and wall temperature distribution were investigated under low mass flux and low pressure conditions in a helically coiled tube with heated length of 7070 mm, outer diameter of 10 mm, inner diameter of 7.6 mm, coil diameter of 300 mm and helical pitch of 40 mm. System pressures, mass fluxes and inlet qualities range from 0.20 to 0.75 MPa, 50 to 260 kg/m(2) s and -0.18 to 0.40, respectively. It was found that the wall temperatures in descending segments of coiled tube were higher than those of climbing ones, while the heat transfer coefficients varied inversely. Around the section circumference, the outside temperature was lower than the inside one: this is more apparent at very low mass flux and pressure conditions. The heat transfer coefficient increases with increasing mass flux, vapor quality and heat flux. However, the pressure has an indeterminate effect. New heat transfer coefficient correlations for current conditions were developed comparing with existing correlations. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:163 / 169
页数:7
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