Investigation of Effects of Heater Tube Angle on the Pool Boiling Heat Transfer Coefficient

被引:0
作者
Khooshehchin, Mohsen [1 ]
Fathi, Sohrab [2 ]
Salimi, Farhad [1 ]
Ovaysi, Saeed [3 ]
机构
[1] Islamic Azad Univ, Kermanshah Branch, Dept Chem Engn, Kermanshah, Iran
[2] Kermanshah Univ Technol, Fac Engn, Dept Chem Engn, Kermanshah, Iran
[3] Razi Univ, Fac Petr & Chem Engn, Kermanshah, Iran
来源
IRANIAN JOURNAL OF CHEMISTRY & CHEMICAL ENGINEERING-INTERNATIONAL ENGLISH EDITION | 2022年 / 41卷 / 03期
关键词
Pool boiling; Heat transfer coefficient; Bubble departure frequency; Bubble departure diameter; Slope of the surface; SURFACE ORIENTATION; DEPARTURE DIAMETER; ROUGHNESS; MODEL; FLUX; ENHANCEMENT; INCLINATION;
D O I
10.30492/ijcce.2021.125265.4095
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
In this experimental study, the effects of slope changes on the heat transfer coefficient in pool boiling in deionized water have been investigated. The experiments were carried out in the average surface roughness of 0.21 mu m on a copper cylinder by changing the surface slope including 0 degrees, 5 degrees, 10 degrees, 15 degrees, 20 degrees, 25 degrees, and 30 degrees. The range of heat flux was from 21 to 77 kW/m in atmospheric conditions. The results indicated that by increasing the heater slope, the departure frequency and bubble departure diameter on the heater surface were increased which lead to an increase in the mixing, turbulence, and heat transfer coefficient. Finally, the slope of 15 degrees has reached the highest heat transfer coefficient with an increase of 20.09% compared to other slopes. Besides the optimized model was mostly overlapped with the experimental results in which Stephan Abdelsalam's model with an average error of 13.9% and the McNelly model with an average error of 24% had the minimum and maximum amount of error among the other models, respectively.
引用
收藏
页码:957 / 970
页数:14
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