Experimental study on condensation heat transfer and pressure drop in horizontal smooth tube for R1234ze(E), R32 and R410A

被引:95
作者
Hossain, Md. Anowar [2 ]
Onaka, Yoji [2 ]
Miyara, Akio [1 ]
机构
[1] Saga Univ, Dept Mech Engn, Saga 8408502, Japan
[2] Saga Univ, Grad Sch Sci & Engn, Saga 8408502, Japan
关键词
Condensation; Heat transfer coefficient; Horizontal tube; Two-phase flow; Pressure drop; TRANSFER COEFFICIENTS; EVAPORATION; MODEL;
D O I
10.1016/j.ijrefrig.2012.01.002
中图分类号
O414.1 [热力学];
学科分类号
摘要
Experimental condensation heat transfer and pressure drop of R1234ze(E), trans-1, 3, 3, 3-tetrafluoropropene (trans-CHF=CHCF3) in a horizontal smooth tube are measured and compared with R32 and the nearly azeotropic HFC refrigerant blend R410A. The effects of mass flux and saturation temperature on heat transfer and pressure drop have been conducted and analyzed. The copper tube with inner diameter of 4.35 mm and length of 3.6 m was used as the test sections. The tests were conducted for mass fluxes varying from 150 to 400 kg (m(-2) s(-1)) and the saturation temperature ranging between 35 and 45 degrees C over the vapor quality range 0.0-1.0. It was found that the experimental heat transfer performance of R1234ze(E) was about 20-45% lower than R32 but 10-30% higher than R410A for saturation temperature 40 degrees C. The experimental results are compared with some well-known existing prediction methods of condensation of pure refrigerant. (C) 2012 Elsevier Ltd and IIR. All rights reserved.
引用
收藏
页码:927 / 938
页数:12
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