New Flow Boiling Heat Transfer Model for Hydrocarbons Evaporating Inside Horizontal Tubes

被引：4
|
作者：
Chen, G. F. [1 ]
Gong, M. Q. [1 ]
Wang, S. [1 ]
Wu, J. F. [1 ]
Zou, X. [1 ]
机构：
[1] Chinese Acad Sci, Tech Inst Phys & Chem, Key Lab Cryogen, Beijing 100190, Peoples R China
来源：
ADVANCES IN CRYOGENIC ENGINEERING | 2014年 / 1573卷
关键词：
Flow Boiling; Heat Transfer; Correlations; Hydrocarbons; Horizontal Tube; GENERAL CORRELATION; VERTICAL TUBES; PRESSURE-DROP; REFRIGERANTS; CHANNELS; DIAMETER; ANNULI; FLUIDS; R-134A; PURE;
D O I：
10.1063/1.4860827
中图分类号：
O414.1 [热力学];
学科分类号：
摘要：
Hydrocarbons have high thermodynamic performances, belong to the group of natural refrigerants, and they are the main components in mixture Joule-Thomson low temperature refrigerators (MJTR). New evaluations of nucleate boiling contribution and nucleate boiling suppression factor in flow boiling heat transfer have been proposed for hydrocarbons. A forced convection heat transfer enhancement factor correlation incorporating liquid velocity has also been proposed. In addition, the comparisons of the new model and other classic models were made to evaluate its accuracy in heat transfer prediction.
引用
收藏
页码：1092 / 1098
页数：7
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