Numerical simulation on the flow and heat transfer characteristics of molten salt nanofluid in the shell-side of helical baffle heat exchangers with elliptic tubes and circular tubes

IF 6.3 2区 材料科学 Q2 ENERGY & FUELS
Junjie Chen , Ziye Ling , Xiaoming Fang , Yuting Wu , Zhengguo Zhang
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引用次数: 0

Abstract

In the energy field, molten salts are widely used due to their excellent heat transfer and thermal storage capabilities. However, there is limited research on the flow and heat transfer characteristics of molten salts in the shell-side of heat exchangers. Helical baffles not only guide the shell-side fluid flow but also reduce flow dead zones, further lowering pressure drop. The elliptic tube, with its streamlined structure, can significantly reduce the shell-side fluid pressure drop and optimize the flow characteristics of molten salts in the shell-side of the heat exchanger. In this study, the flow and heat transfer characteristics of molten salt nanofluid in helical baffle heat exchangers with elliptic tube and circular tube were investigated through numerical simulations. The results show that the heat transfer rate in elliptic tube heat exchanger increases by 5.45 %–8.51 %, the pressure drop is 56.55 % of that of the circular tubes, and the heat transfer coefficient per unit pressure drop is 1.85 times higher in elliptic tube heat exchanger. The comprehensive thermal performance factor (TPF) of the elliptic tube is 1.39 on average, indicating that elliptic tubes can improve the comprehensive performance of the heat exchanger, enhancing heat transfer while optimizing fluid flow. The research on the helical baffle heat exchanger with elliptic tubes presented in this paper provides valuable references for the design of future molten salt heat exchangers.
椭圆管和圆管螺旋折流板换热器壳侧熔盐纳米流体流动和换热特性的数值模拟
在能源领域,熔盐因其优良的传热和蓄热能力而得到广泛应用。然而,对熔盐在换热器壳侧的流动和换热特性的研究有限。螺旋挡板既能引导壳侧流体流动,又能减小流动死区,进一步降低压降。椭圆管采用流线型结构,可以显著降低壳侧流体压降,优化熔盐在换热器壳侧的流动特性。本文通过数值模拟研究了熔盐纳米流体在椭圆管和圆管螺旋折流板换热器中的流动和换热特性。结果表明,椭圆管换热器的换热率提高了5.45% ~ 8.51%,压降是圆管换热器的56.55%,单位压降换热系数是圆管换热器的1.85倍。椭圆管的综合热性能因子(TPF)平均为1.39,表明椭圆管可以提高换热器的综合性能,在优化流体流动的同时加强传热。本文对椭圆管螺旋折流板换热器的研究为今后熔盐换热器的设计提供了有价值的参考。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
Solar Energy Materials and Solar Cells
Solar Energy Materials and Solar Cells 工程技术-材料科学:综合
CiteScore
12.60
自引率
11.60%
发文量
513
审稿时长
47 days
期刊介绍: Solar Energy Materials & Solar Cells is intended as a vehicle for the dissemination of research results on materials science and technology related to photovoltaic, photothermal and photoelectrochemical solar energy conversion. Materials science is taken in the broadest possible sense and encompasses physics, chemistry, optics, materials fabrication and analysis for all types of materials.
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