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首页> 外文期刊>International Journal of Heat and Mass Transfer >Heat transfer performance of the pin-fin heat sink filled with packed brass beads under a vertical oncoming flow
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Heat transfer performance of the pin-fin heat sink filled with packed brass beads under a vertical oncoming flow

机译:垂直迎面流下填充黄铜珠的针翅式散热器的传热性能

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This study experimentally investigated the fluid flow and heat transfer characteristics of the pin-fin heat sink fully filled with packed brass beads under a vertical oncoming air flow. The dimensions of the pin-fin heat sink were fixed. A constant heat flux was applied on the bottom of the heat sink. The pin-fin heat sinks of various pin-fin side lengths and pin-fin interval spaces filled with brass beads of various diameters would result in different porous properties, leading the corresponding changes in the behaviors of the fluid flow and heat transfer. The results indicated that, for the same Reynolds number (Re) of oncoming flow, the pin-fin heat sinks with packed brass beads (Group 3) have significant heat transfer gains (17.0-78.4% and 95.8-311.2% at Re = 10,000, respectively) by comparing with the corresponding pure pin-fin heat sinks (Group 1) and pure packed-brass-beads heat sinks (Group 2). The Nusselt-number empirical formula of the Group 3 heat sink was provided in some superposition form of the Group 1 heat sink and Group 2 heat sink. The heat-transfer superposition effect fell remarkably when the porosity of the Group 3 heat sink was notably lower than those of the corresponding Group 1 heat sink and Group 2 heat sink. Besides, based on the same dimensionless pumping power, the Group 3 heat sink generally has higher heat transfer performance than the corresponding Group 1 heat sink and Group 2 heat sink, except a few exceptions at smaller dimensionless pumping power.
机译:这项研究通过实验研究了在垂直迎面而来的气流下充满了填充黄铜珠的针翅式散热器的流体流动和传热特性。针翅式散热器的尺寸是固定的。在散热器的底部施加恒定的热通量。针状翅片侧面长度各不相同的针状翅片散热器和填充有各种直径的黄铜珠的针状翅片间隔空间将导致不同的多孔性,从而导致流体流动和传热行为的相应变化。结果表明,对于相同的雷诺数(Re)的来流,带有填充黄铜珠的针翅式散热器(第3组)具有显着的传热增益(Re = 10,000时为17.0-78.4%和95.8-311.2%) ,分别与相应的纯针翅式散热器(第1组)和纯黄铜管珠状散热器(第2组)进行比较。第3组散热器的Nusselt数经验公式以第1组散热器和第2组散热器的某种叠加形式提供。当第3组散热器的孔隙率显着低于相应的第1组散热器和第2组散热器的孔隙率时,传热叠加效果显着下降。此外,基于相同的无量纲泵浦功率,第3组散热器通常比相应的第1组散热器和第2组散热器具有更高的传热性能,但在较小的无量纲泵浦功率方面除外。

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