Experimental investigation on flow condensation of methane in a horizontal smooth tube

被引:44
|
作者
Zhuang, X. R. [1 ,2 ]
Chen, G. F. [1 ]
Zou, X. [1 ]
Song, Q. L. [1 ,2 ]
Gong, M. Q. [1 ]
机构
[1] Chinese Acad Sci, Tech Inst Phys & Chem, Key Lab Cryogen, Beijing 100190, Peoples R China
[2] Univ Chinese Acad Sci, Beijing 100049, Peoples R China
基金
中国国家自然科学基金;
关键词
Condensation; Flow pattern; Heat transfer; Pressure drop; Temperature difference; Methane; FRICTIONAL PRESSURE-DROP; HEAT-TRANSFER; 2-PHASE FLOW; AIR-WATER; PATTERN; REFRIGERANTS; R134A; R170;
D O I
10.1016/j.ijrefrig.2017.03.021
中图分类号
O414.1 [热力学];
学科分类号
摘要
An experimental investigation on flow visualization of adiabatic and condensation conditions as well as condensation heat transfer coefficient and pressure drop of methane in a horizontal smooth tube was carried out. The tests were conducted at saturation pressure of 2-3.5 MPa with mass flux of 99-255 kg m(-2) s(-1) and fluid-to-wall temperature difference of 4.8-20.2 K throughout the vapor quality range. The effects of mass flux, saturation pressure, vapor quality and temperature difference were studied and discussed. In order to expand the range of temperature difference, some condensation heat transfer coefficients of ethane with larger temperature differences (19.7-39.2 K) were also reported in this paper. The experimental data were compared with many well-known correlations of condensation heat transfer coefficient and pressure drop. An improved heat transfer correlation for different flow patterns was proposed and predicted the experimental results well with a mean absolute relative deviation of 6.86%. (C) 2017 Elsevier Ltd and IIR. All rights reserved.
引用
收藏
页码:193 / 214
页数:22
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