Two-phase heat transfer and pressure drop of LNG during saturated flow boiling in a horizontal tube

被引:13
作者
Chen, Dongsheng [1 ]
Shi, Yumei [1 ]
机构
[1] Shanghai Jiao Tong Univ, Sch Mech Engn, Inst Refrigerat & Cryogen, Shanghai 200240, Peoples R China
关键词
Flow boiling; Heat transfer; LNG; Mixture; GENERAL CORRELATION; TRANSFER MODEL; PATTERN MAP; REFRIGERANTS; MIXTURES; PURE;
D O I
10.1016/j.cryogenics.2013.09.010
中图分类号
O414.1 [热力学];
学科分类号
摘要
Two-phase heat transfer and pressure drop of LNG (liquefied natural gas) have been measured in a horizontal smooth tube with an inner diameter of 8 mm. The experiments were conducted at inlet pressures from 0.3 to 0.7 MPa with a heat flux of 8-36 kW m(-2), and mass flux of 49.2-201.8 kg m(-2) S-1. The effect of vapor quality, inlet pressure, heat flux and mass flux on the heat transfer characteristic are discussed. The comparisons of the experimental data with the predicted value by existing correlations are analyzed. Zou et al. (2010) correlation shows the best accuracy with 24.1% RMS deviation among them. Moreover four frictional pressure drop methods are also chosen to compare with the experimental database. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:45 / 54
页数:10
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