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A numerical investigation of turbulent convective heat transfer of supercritical CO_2 in vertical mini tubes

机译:立式微型管中超临界CO_2湍流对流换热的数值研究

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This article presents a numerical investigation on the turbulent convective heat transfer of supercritical CO_2 in vertical mini tubes. For buoyancy-aided cases, buoyancy-opposed cases and buoyancy-free cases, the profiles of velocity, temperature and turbulent kinetic energy, as well as heat transfer coefficients and Nusselt numbers inside the tubes with the diameters less than 2 mm, under heating and cooling conditions, are obtained. It is found that the buoyancy is significant near the pseudocritical point due to the sharply varied properties of supercritical CO_2, leading to the variations of the flow pattern, turbulent production and hence heat transfer coefficient in the tube. Detailed explanations to the physics of the complex but interesting transport phenomena are given. Furthermore, the values of the buoyancy parameter Gr_b/Re_b~(2.7) are calculated, and Jackson and Hall's criterion for assessing the buoyancy's influence is examined for cooling flows in mini tubes.
机译:本文提出了在垂直微型管中超临界CO_2湍流对流换热的数值研究。对于有浮力的情况,有浮力的情况和无浮力的情况,在加热和加热条件下,直径小于2 mm的管内的速度,温度和湍动能以及传热系数和Nusselt数的分布图获得冷却条件。发现由于超临界CO 2的特性急剧变化,在伪临界点附近的浮力很大,从而导致流型,湍流产生以及管中的传热系数的变化。给出了对复杂但有趣的传输现象的物理学的详细解释。此外,计算浮力参数Gr_b / Re_b〜(2.7)的值,并对微型管中的冷却流检查杰克逊和霍尔的评估浮力影响的标准。

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