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Numerical Solution of Mixed Convective Heat Transfer of Supercritical Carbon Dioxide in Horizontal Miniature Tubes

机译:水平微型管中超临界二氧化碳混合对流传热的数值解

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The investigation of laminar mixed convection with heat and mass transfer of supercritical carbon dioxide in horizontal miniature tubes was performed numerically. The flow patterns, isotherms, distributions of wall shear stresses and Nusselt numbers in typical cross sections with tube diameters less than 1.0 mm under both cooling and heating conditions with and/or without gravity were obtained. The variations of skin-friction coefficients, heat transfer coefficients and Nusselt numbers with bulk temperature were also provided. The results presented in this paper reveal that the buoyancy effects on supercritical carbon dioxide laminar flow and heat transfer in horizontal miniature tubes are significant, where the secondary motions in cross sections are very severe due to the sharply varied physical properties of supercritical fluid. The results of this work are of significance for the design of high efficiency compact heat exchangers of supercritical carbon dioxide.
机译:在数值上进行了用水平微型管中的超临界二氧化碳的热量和传质对流的研究。 获得了在冷却和加热条件下小于1.0mm的管直径小于1.0mm的典型横截面的流动模式,等温,壁剪切应力的分布,并且在带有和/或没有重力的情况下,横截面。 还提供了具有批量温度的皮肤摩擦系数,传热系数和氮数数的变化。 本文提出的结果表明,水平微型管中超临界二氧化碳层流和传热的浮力效应是显着的,其中由于超临界流体的急剧各种物理性质,横截面的二次运动非常严重。 这项工作的结果对于超临界二氧化碳的高效率紧凑型热交换器的设计具有重要意义。

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