Heat transfer characteristics of steam condensation flow in vacuum horizontal tube

被引:13
|
作者
Wang, Yaoxuan [1 ]
Mu, Xingsen [1 ]
Shen, Shengqiang [1 ]
Zhang, Wenjie [1 ]
机构
[1] Dalian Univ Technol, Sch Energy & Power Engn, Key Lab Liaoning Prov Desalinat, Dalian, Peoples R China
基金
美国国家科学基金会;
关键词
Condensation; Horizontal tube; Heat transfer coefficient; PRESSURE-DROP; SMOOTH TUBE; TRANSFER COEFFICIENTS; R410A; REFRIGERANTS; R32; R22;
D O I
10.1016/j.ijheatmasstransfer.2016.12.006
中图分类号
O414.1 [热力学];
学科分类号
摘要
The heat transfer characteristics of steam condensation flow in a vacuum horizontal long tube were studied experimentally when the saturation temperature varies from 50 to 70 degrees C, mass flow rate is no more than 11 kg/(m(2) s) and temperature differences between steam and cooling water are 3, 5 and 7 degrees C respectively. The results of experiments indicate that the steam temperature decreases and the condensation temperature difference decreases first and then increases along the flow direction. The effects of mass flow rate and total temperature difference on temperature distribution are also discussed in the paper. The condensation heat transfer coefficient increases first and then decreases along the flow direction. The heat transfer coefficient increases with mass flow rate in most cases, but may decrease in the first section at high mass flow rate. The heat transfer coefficient also increases with saturation temperature and decreases with condensation temperature difference. The heat transfer rate decreases along the flow direction and increases with mass flow rate. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:128 / 135
页数:8
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