Two-phase pressure drop of ammonia in horizontal small diameter tubes: Experiments and correlation

被引:4
|
作者
Gao, Yuping [1 ,2 ]
Feng, Ye [3 ]
Shao, Shuangquan [1 ,2 ]
Tian, Changqing [1 ,2 ,4 ]
机构
[1] Tech Inst Phys & Chem, CAS Key Lab Cryogen, Beijing 100190, Peoples R China
[2] Chinese Acad Sci, Beijing Key Lab Thermal Sci & Technol, Tech Inst Phys & Chem, Beijing 100190, Peoples R China
[3] Changsha Univ Sci & Technol, Coll Energy & Power Engn, Changsha 410114, Hunan, Peoples R China
[4] Univ Chinese Acad Sci, Beijing 100049, Peoples R China
基金
中国国家自然科学基金; 国家重点研发计划;
关键词
Ammonia; Two-phase flow; Pressure drop; Prediction correlation; HEAT-TRANSFER; FLOW; SMOOTH; PREDICTION; VAPORIZATION; REFRIGERANTS; GRADIENTS; CHANNELS; FRICTION; CO2;
D O I
10.1016/j.ijrefrig.2018.11.018
中图分类号
O414.1 [热力学];
学科分类号
摘要
A series of experiments are conducted to investigate the two-phase pressure drop of ammonia in horizontal small diameter tube. The experiments are performed at saturation temperatures of -15.8-4.6 degrees C, and the mass flux range is from 20 to 100 kg m(-2) s(-1). This paper analyzes the influence mechanisms of vapor quality, mass flux, saturation temperature, and tube diameter on the two-phase frictional pressure gradient in detail. Meanwhile, several correlations are compared with all the experimental data and the results show that the Muller-Steinhagen and Heck (1986) correlation gives the best agreement. With the analysis of the major forces for ammonia two-phase flow under the tested experimental conditions, the Reynolds number and Bond number are introduced to modify the Muller-Steinhagen and Heck (1986) correlation. Lastly, a modified correlation is developed with the mean absolute deviation of only 13.5%, and 89.2% of the data are within the +/- 30% error band. In addition, the modified correlation is evaluated based on a complied database which contains 951 experimental data points from 11 published literatures. (C) 2018 Elsevier Ltd and IIR. All rights reserved.
引用
收藏
页码:283 / 293
页数:11
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