储能科学与技术 ›› 2020, Vol. 9 ›› Issue (4): 1091-1097.doi: 10.19799/j.cnki.2095-4239.2020.0020

• 储能材料与器件 • 上一篇    下一篇

低熔点四元硝酸盐圆管内受迫对流换热特性

张春雨(), 郭航(), 吴玉庭, 张灿灿, 叶芳, 马重芳   

  1. 北京工业大学环境与能源工程学院,传热强化与过程节能教育部重点实验室及传热与能源利用北京市重点实验室,北京 100124
  • 收稿日期:2020-01-07 修回日期:2020-01-19 出版日期:2020-07-05 发布日期:2020-06-30
  • 通讯作者: 郭航 E-mail:zhangchunyu2017@emails.bjut.edu.cn;hangguo@bjut.edu.cn
  • 作者简介:张春雨(1995—),男,硕士研究生,主要研究方向为熔盐及熔盐纳米流体受迫对流换热,E-mail:zhangchunyu2017@emails.bjut.edu.cn
  • 基金资助:
    国家重点研发计划项目(2017YFB0903603)

Forced convection heat transfer characteristics in a circular tube with low-melting-point quaternary nitrate

ZHANG"Chunyu(), GUO"Hang(), WU"Yuting, ZHANG"Cancan, YE"Fang, MA"Chongfang   

  1. Ministry of Education Key Laboratory of Enhanced Heat Transfer and Energy Conservation, Beijing Key Laboratory of Heat Transfer and Energy Conversion, College of Environmental and Energy Engineering, Beijing University of Technology, Beijing 100124, China
  • Received:2020-01-07 Revised:2020-01-19 Online:2020-07-05 Published:2020-06-30
  • Contact: Hang GUO E-mail:zhangchunyu2017@emails.bjut.edu.cn;hangguo@bjut.edu.cn

摘要:

为了验证经典对流换热关联式对于新型的低熔点四元硝酸盐的适用性,该文研究了不同工况下低熔点四元混合硝酸盐在套管式换热器内的受迫对流换热特性。通过套管式换热器内管中的熔盐与壳侧的导热油的换热实验,测量得到熔盐与导热油在套管式换热器实验段的进出口温度,并获得了熔盐与导热油的总传热系数。通过威尔逊分离法从总传热系数中分离得到熔盐侧的对流换热系数,从而研究圆管中熔盐的对流换热特性。结果表明:该低熔点四元盐在研究的充分发展紊流区域内,其雷诺数在1×104~5×104之间,普朗特数在4.9~15.5之间,熔盐和导热油的总换热系数在670~1300 W/(m2·K)之间,熔盐侧的对流换热系数在2900~7800 W/(m2·K)之间变化。根据实验数据拟合得出了低熔点四元盐在圆管中紊流段的对流换热关联式。将实验数据与经典的对流关联式比较发现,经典关联式仍然适用于低熔点四元混合硝酸盐的管内对流换热。该研究为熔融盐在太阳能热发电中的实际应用提供了参考数据。

关键词: 熔融盐, 受迫对流, 传热, 紊流段

Abstract:

The forced convection heat transfer characteristics of a low-melting-point quaternary nitrate in a tube-type heat exchanger are studied under different conditions to verify the applicability of the classical convection heat transfer correlation in this case. Based on the heat transfer experiment of the molten salt in the inner tube and the heat transfer oil on the shell side of the tube-type heat exchanger, the inlet and outlet temperatures of the molten salt and heat transfer oil in the test section of the tube-type heat exchanger are obtained. Further, the total heat transfer coefficients of the molten salt and heat transfer oil are obtained. Using the Wilson separation method, the convective heat transfer coefficient on the molten salt side is obtained from the total heat transfer coefficient to study the convective heat transfer characteristics of molten salt in a circular tube. Results show that the Reynolds number of the low-melting-point quaternary salt is 1 × 104—5 × 104, the Prandtl number is 4.9—15.5, and the total heat transfer coefficient of the molten salt and the heat transfer oil is 670—1300 W·m-2·K-1 in the fully developed turbulent region. The convective heat transfer coefficient on the molten salt side is 2900—7800 W·m-2·K-1. Subsequently, the correlation between convection and heat transfer in case of the low-melting-point quaternary salt in the turbulent section of the tube is obtained according to the experimental data. By comparing the experimental data with the classical convection correlations, the classical convection correlation is observed to be still applicable to convection heat transfer in a tube containing low-melting-point quaternary nitrate. This study provides reference data for the practical application of molten salt in solar thermal power generation.

Key words: molten salt, forced convection, heat transfer, turbulent section

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