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Numerical investigation on conjugate cooling heat transfer to supercritical CO2 in vertical double-pipe heat exchangers

机译:立式双管换热器中共轭冷却传热至超临界CO2的数值研究

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摘要

Conjugate cooling heat transfer to supercritical CO2 in a vertical double-pipe heat exchanger was numerically investigated in the present study. With the aim to better understand the conjugate cooling mechanism of supercritical fluid, detailed information on heat transfer behavior is provided. The results demonstrate that the numerical results predicted by the Abe, Kondoh, and Nagano (AKN) model show the best agreement with the experimental data. After validation, the influences of cooling water Re and temperature at the shell side, supercritical fluid Re at the tube side, flow direction, and pipe diameter on conjugate cooling heat transfer were investigated based on velocity fields. We conclude that cool water Re and temperature at the shell side have a significant effect on the cooling phenomenon at the tube side. Reduction in heat transfer could be avoided by either an increase in Re-CO2 or a decrease in d(i). In addition, variations in density and c(p) are the most significant factors to determine the occurrence of abnormal heat transfer phenomena. In comparison with the heating process of supercritical CO2, the sharply increased viscosity noted would hinder the distortion of the flow field to ameliorate heat transfer deterioration during the cooling process.
机译:在本研究中,通过数值研究了在立式双管热交换器中将共轭冷却热传递给超临界CO2。为了更好地了解超临界流体的共轭冷却机理,提供了有关传热行为的详细信息。结果表明,由安倍晋三和长野(AKN)模型预测的数值结果与实验数据显示出最好的一致性。验证后,基于速度场研究了冷却水Re和壳侧温度,管侧超临界流体Re,流向和管径对共轭冷却传热的影响。我们得出的结论是,壳侧的冷水Re和温度对管侧的冷却现象有重大影响。可以通过增加Re-CO2或减少d(i)来避免热量传递的减少。此外,密度和c(p)的变化是确定异常传热现象发生的最重要因素。与超临界CO2的加热过程相比,注意到的急剧增加的粘度将阻碍流场的变形,从而改善冷却过程中的传热恶化。

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