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Effect of secondary flows due to buoyancy and contraction on heat transfer in a two-section plate-fin heat sink

机译:浮力和收缩引起的二次流对两段式板翅式散热器的传热的影响

摘要

The effect of buoyancy forces on laminar heat transfer inside a variable width plate-fin heat sink is numerically analyzed: the configuration under investigation comprises an array of rectangular fins, the number of which is doubled at the streamwise middle length of the plate, leading to a stepwise reduction in the respective channel width and hydraulic diameter. The mixed convection problem is thoroughly examined for Archimedes numbers in the range Ar = 1.32-5.82 and Reynolds numbers, based on the channel hydraulic diameter before the stepwise reduction, in the range Re = 559-667, under the thermal boundary condition of axially constant heat flux. It is illustrated that the secondary flow pattern emanating from the flow contraction and manifested through the presence of a pair of counter-rotating horseshoe vortices and a pair of counter-rotating (fin) sidewall vortices interacts with longitudinal rolls created by buoyancy forces. In fact, the lower horseshoe vortices that are co-rotating with the buoyancy-induced rolls are significantly enhanced in magnitude and cause intense fluid mixing in the vicinity of the channel bottom wall, with a substantial distortion of the temperature field. The numerical results indicate that the joint action of the buoyancy-induced rolls and the combined secondary flow pattern has a beneficial impact on the heat sink thermal performance, a fact quantified through the circumferentially-averaged local Nusselt number distributions. The effect of the top lid thermal conductivity on the heat transfer inside the heat sink is also discussed. Finally, a comparative investigation is conducted between the present variable-channel-width configuration and two configurations of fixed-width heat sink designs. The comparative results reveal that the introduction of stepwise channels leads to superior heat transfer performance, i.e. lower values of the total thermal resistance with mitigated pressure drop penalty and increased temperature uniformity on the cooled surface.
机译:数值分析了浮力对可变宽度板翅式散热器内部层流传热的影响:所研究的结构包括矩形翅片阵列,矩形翅片的数量在板的流向中间长度处增加了一倍,从而导致逐步减小各自的通道宽度和水力直径。在轴向恒定的热边界条件下,基于逐步减小之前的通道水力直径,在范围Ar = 1.32-5.82的阿基米德数和雷诺数的Re = 559-667范围内,彻底检查了混合对流问题热通量。示出了由流动收缩产生并通过一对反向旋转的马蹄形涡流和一对反向旋转的(翅片)侧壁涡流的存在而显现的次级流动模式与由浮力产生的纵向辊相互作用。实际上,与浮力引起的辊共同旋转的下部马蹄形涡流的幅度显着增强,并在通道底壁附近引起强烈的流体混合,从而使温度场明显变形。数值结果表明,由浮力引起的辊和组合的二次流模式的共同作用对散热器的热性能具有有益的影响,这一事实是通过沿周向平均的局部努塞尔特分布进行量化的。还讨论了顶盖导热率对散热器内部传热的影响。最后,在目前的可变通道宽度配置和固定宽度散热器设计的两种配置之间进行了比较研究。比较结果表明,阶梯状通道的引入导致优异的传热性能,即较低的总热阻值,同时减轻了压降损失,并提高了冷却表面的温度均匀性。

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