Numerical simulation of heat transfer performance and convective vortex evolution in a phase change thermal storage device with dispersed heat sources

IF 1.7 4区 工程技术 Q3 MECHANICS
Jianlong Zi, Wei Long, Yunlong Liu, Tingting Lin
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Abstract

A numerical model based on the enthalpy method for solidification/melting that incorporates liquid-phase convection was established for a shell-and-tube phase-change thermal energy storage device with dispersed heat sources. This model optimized the heat source structure and simulated the phase change process, thermal storage performance, and evolution and effects of convection-induced vortices. To overcome the limitations of melting blind spots in traditional inner-tube heat sources, a dispersed heating approach was introduced to optimize the heat source distribution on the inner and outer tubes without changing the heat exchange area. The optimal heat source model demonstrated superior heat transfer performance, featuring an inner-tube top heat source and three uniformly distributed outer-tube bottom heat sources at a dispersion angle of 60°. It reduced the complete melting time by 70.88% compared to the inner-tube heat source alone and by 51.99% compared to the outer-tube bottom heat source. The dispersed heat sources effectively utilized the natural convection benefits at the upper inner side and enhanced the heat transfer at the lower sections to address the melting blind spots of the central heat source, thereby improving the uniformity of the process. The enhancement in heat transfer within the dispersed heat source model is primarily due to the optimized heat source distribution, which facilitates a more dispersed and uniform vortex evolution during the phase change. This promotes the development of the liquid-solid interface and reduces the mutual interference in convection vortex expansion. Hence, the internal heat transfer rate and thermal storage capacity of the system are improved.

Abstract Image

对带有分散热源的相变蓄热装置的传热性能和对流漩涡演化进行数值模拟
针对具有分散热源的壳管式相变热能储存装置,建立了一个基于凝固/熔化焓法的数值模型,其中包含液相对流。该模型优化了热源结构,模拟了相变过程、热存储性能以及对流引起的涡流的演变和影响。为了克服传统内管热源存在熔化盲点的局限性,研究人员引入了一种分散加热方法,在不改变热交换面积的情况下优化热源在内外管上的分布。最佳热源模型显示出卓越的传热性能,其特点是一个内管顶部热源和三个均匀分布的外管底部热源,分散角为 60°。与单独使用内管热源相比,完全熔化时间缩短了 70.88%,与使用外管底部热源相比,完全熔化时间缩短了 51.99%。分散热源有效利用了内侧上部的自然对流优势,并增强了下部的热传递,解决了中央热源的熔化盲点,从而提高了工艺的均匀性。分散热源模型传热效果的增强主要归功于优化的热源分布,这有利于在相变过程中形成更加分散和均匀的涡流演化。这促进了液固界面的发展,减少了对流涡旋扩展的相互干扰。因此,系统的内部传热速率和蓄热能力都得到了提高。
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来源期刊
Heat and Mass Transfer
Heat and Mass Transfer 工程技术-力学
CiteScore
4.80
自引率
4.50%
发文量
148
审稿时长
8.0 months
期刊介绍: This journal serves the circulation of new developments in the field of basic research of heat and mass transfer phenomena, as well as related material properties and their measurements. Thereby applications to engineering problems are promoted. The journal is the traditional "Wärme- und Stoffübertragung" which was changed to "Heat and Mass Transfer" back in 1995.
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