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首页> 外文期刊>International Journal of Heat and Mass Transfer >Heat transfer enhancement of Taylor-Couette-Poiseuille flow in an annulus by mounting longitudinal ribs on the rotating inner cylinder
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Heat transfer enhancement of Taylor-Couette-Poiseuille flow in an annulus by mounting longitudinal ribs on the rotating inner cylinder

机译:通过在旋转的内部圆柱体上安装纵向肋,增强环空中泰勒-库埃特-泊瓦流的传热

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This work experimentally investigates the heat transfer characteristics of Taylor-Couette-Poiseuille flow in an annular channel by mounting longitudinal ribs on the rotating inner cylinder. The ranges of the axial Reynolds number (Re) and the rotational Reynolds number (Re_Ω) are Re = 30-1200 and Re_Ω = 0-2922, respectively. Three modes of the inner cylinder without/with longitudinal ribs are considered. A special entry and exit design for the axial coolant flow reveals some interesting findings. The value of Nusselt number (Nu) is almost minimal at the inlet of the annular channel, and then sharply rises in the axial direction. The average Nusselt number (Nu) increases with Re. Nu increases rapidly with Re_Ω at low Re (such as at Re = 30 and 60) but that the effect of Re_Ω decreases as the value increases (such as at Re = 300-1200). The ratio Nu/Nu_0 increases with Re_Ω and exceed two at all Re and in the test modes. The heat transfer is typically promoted by mounting longitudinal ribs on the rotating inner cylinder, especially at Re = 300 and 600. When Re = 300 or 600 and Re_Ω > 2000, the Nu of the system with ribs reaches around 1.4 times that of Nu_A (Nu in mode A). Under a given pumping power constraint (PRe~3), the Nu of the system with ribs (modes B and C) generally exceeds that without ribs (mode A), while the difference between the values of Nu in modes B and A slowly falls as PRe~3 increases. Additionally, mode B (with ribs) is preferred for high heat transfer when PRe~3 < 4.5 x 10~(13) but mode C (with cavities on ribs) is optimal for high heat transfer when PRe~3 > 4.5 x 10~(13).
机译:这项工作通过在旋转的内筒上安装纵向肋来实验性地研究环形通道中Taylor-Couette-Poiseuille流的传热特性。轴向雷诺数(Re)和旋转雷诺数(Re_Ω)的范围分别为Re = 30-1200和Re_Ω= 0-2922。考虑了没有/有纵向肋的内圆柱体的三种模式。轴向冷却剂流的特殊入口和出口设计揭示了一些有趣的发现。努塞尔数(Nu)的值在环形通道的入口处几乎是最小的,然后沿轴向急剧上升。平均Nusselt数(Nu)随着Re的增加而增加。当Re_Ω在低Re时(例如Re = 30和60),Nu迅速增加(但Re_Ω的影响随该值的增加而减小)(例如Re = 300-1200)。 Nu / Nu_0的比率随Re_Ω增大,在所有Re和测试模式下均超过2。通常通过在旋转的内部圆柱体上安装纵向肋来促进热传递,尤其是在Re = 300和600时。当Re = 300或600且Re_Ω> 2000时,带有肋的系统的Nu约为Nu_A的1.4倍( Nu在模式A中)。在给定的泵浦功率约束下(PRe〜3),带肋的系统(模式B和C)的Nu值通常超过不带肋的系统(模式A),而模式B和A的Nu值之差缓慢下降随着PRe〜3的增加。此外,当PRe〜3 <4.5 x 10〜(13)时,模式B(带有肋)是高传热的首选,而当PRe〜3> 4.5 x 10〜(13)时,模式C(带有肋的腔室)对于高传热是最佳的。 (13)。

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