Convective heat transfer characteristics in the turbulent region of molten salt in concentric tube

被引:19
|
作者
Chen, Y. S. [1 ,2 ]
Wang, Y. [1 ,2 ]
Zhang, J. H. [1 ,2 ]
Yuan, X. F. [1 ,2 ]
Tian, J. [1 ,2 ]
Tang, Z. F. [1 ,2 ]
Zhu, H. H. [1 ,2 ]
Fu, Y. [1 ,2 ]
Wang, N. X. [1 ,2 ]
机构
[1] Chinese Acad Sci, Shanghai Inst Appl Phys, Shanghai 201800, Peoples R China
[2] Chinese Acad Sci, Key Lab Nucl Radiat & Nucl Energy Technol, Shanghai 201800, Peoples R China
基金
中国国家自然科学基金;
关键词
Molten salt; Convective heat transfer; Heat exchanger; Concentric tube; Heat transfer correlation; PRESSURE-DROP; REACTOR; TRANSITION;
D O I
10.1016/j.applthermaleng.2015.12.023
中图分类号
O414.1 [热力学];
学科分类号
摘要
In order to better understand the heat transfer behavior and characteristics of molten salt in heat exchanger, the convective heat transfer characteristics of molten salt in salt-to-oil concentric tube are studied. Overall heat transfer coefficients of the heat exchanger are calculated using Wilson plots. Heat transfer coefficients of tube side molten salt with the range of Reynolds number from 10,000 to 50,000 and the Prandtl number from 11 to 27 are evaluated invoking the calculated overall heat transfer coefficients. The effects of velocity and temperature on the convective heat transfer in the turbulent region of molten salt are studied by comparing with the traditional correlations. The results show that the heat transfer characteristics of molten salt are in line with the empirical heat transfer correlation; however, Dittus-Boelter, Gnielinski, Sieder-Tate and Hausen correlations all give a larger deviation for the experimental data. Finally, based on the experimental data and Sieder-Tate correlation, a modified heat transfer correlation is proposed and good agreement is observed between the experimental data and the modified correlation. The results will also provide an important reference for the design of the heat exchangers in the Thorium-based Molten Salt Reactor. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:213 / 219
页数:7
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