Study on the effect of the porous media equivalent particulate fouling model on heat transfer performance in heat exchanger channels

IF 6.9 2区 工程技术 Q2 ENERGY & FUELS Applied Thermal Engineering Pub Date : 2025-05-01 Epub Date: 2025-01-23 DOI:10.1016/j.applthermaleng.2025.125709
Jiang Li, Zhimin Han, Wei Liu, Taozhi Wang, Hongliang Chang
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Abstract

With the development of modern industry, the issue of particulate fouling deposition within heat exchanger channels has become increasingly severe, significantly reducing heat transfer coefficient and potentially leading to hazards such as tube rupture and low efficiency. To investigate the impact of particulate fouling on heat transfer performance in heat exchanger channels, this paper proposes a porous media equivalent particulate fouling model, which has been experimentally validated for accuracy. The model is applied to both smooth and complex heat exchanger channels, with a comparative analysis focusing on the changes in fouling resistance and Nusselt number between the porous media equivalent particulate fouling model and the traditional particulate fouling model. Additionally, the study provides a detailed examination of the effect of fouling layer thickness on heat transfer performance in complex channels. The results indicate that the simulation results using the porous media equivalent particulate fouling model show a higher correlation with experimental data, with the average error reduced by 5.48 %. In both smooth and complex heat exchanger channels, fouling resistance increases progressively along the channel, while the Nusselt number decreases. In the complex channel, due to the influence of vortex generators, fouling resistance and Nusselt number exhibit periodic variations. When the porous media equivalent particulate fouling model is used, the obstruction effect of the fouling layer on the flow field is considered, resulting in a significant increase in fouling resistance, which in turn reduces the Nusselt number. Furthermore, in the complex channel, as particle concentration increases, the fouling layer thickness gradually increases. When the fouling layer reaches a thickness of 0.42 mm, the heat transfer efficiency decreases by 12.1 %, while flow resistance increases by 36.0 %.
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多孔介质等效颗粒结垢模型对换热器通道传热性能影响的研究
随着现代工业的发展,换热器通道内颗粒污垢沉积问题日益严重,大大降低了换热系数,并可能导致管道破裂、效率低下等危害。为了研究颗粒结垢对换热器通道传热性能的影响,本文提出了多孔介质等效颗粒结垢模型,并通过实验验证了该模型的准确性。将该模型应用于光滑换热器通道和复杂换热器通道,重点对比分析多孔介质等效颗粒结垢模型与传统颗粒结垢模型的结垢阻力和努塞尔数变化。此外,该研究还详细研究了污垢层厚度对复杂通道传热性能的影响。结果表明,采用多孔介质等效颗粒结垢模型的模拟结果与实验数据具有较高的相关性,平均误差减小了5.48%。在光滑和复杂的换热器通道中,污垢阻力沿通道逐渐增大,而努塞尔数减小。在复杂通道中,由于涡发生器的影响,结垢阻力和努塞尔数呈现周期性变化。采用多孔介质等效颗粒结垢模型时,考虑了结垢层对流场的阻碍作用,导致结垢阻力显著增大,进而降低了努塞尔数。此外,在复杂通道中,随着颗粒浓度的增加,污染层厚度逐渐增加。当污垢层厚度达到0.42 mm时,传热效率降低12.1%,流动阻力增加36.0%。
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来源期刊
Applied Thermal Engineering
Applied Thermal Engineering 工程技术-工程:机械
CiteScore
11.30
自引率
15.60%
发文量
1474
审稿时长
57 days
期刊介绍: Applied Thermal Engineering disseminates novel research related to the design, development and demonstration of components, devices, equipment, technologies and systems involving thermal processes for the production, storage, utilization and conservation of energy, with a focus on engineering application. The journal publishes high-quality and high-impact Original Research Articles, Review Articles, Short Communications and Letters to the Editor on cutting-edge innovations in research, and recent advances or issues of interest to the thermal engineering community.
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