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Fluid flow and heat transfer characteristics of low temperature two-phase micro-channel heat sinks - Part 2. Subcooled boiling pressure drop and heat transfer

机译:低温两相微通道散热器的流体流动和传热特性-第2部分。过冷沸腾压降和传热

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摘要

This second part of a two-part study explores the performance of a new cooling scheme in which the primary working fluid flowing through a micro-channel heat sink is indirectly cooled by a refrigeration cooling system. The objective of this part of study is to explore the pressure drop and heat transfer characteristics of the heat sink. During single-phase cooling, pressure drop decreased with increasing heat flux because of decreased liquid viscosity. However, pressure drop began increasing with increasing heat flux following bubble departure. These opposite trends produced a minimum in the variation of pressure drop with heat flux. Increasing liquid subcooling decreased two-phase pressure drop because of decreased void fraction caused by strong condensation at bubble interfaces as well as decreased likelihood of bubble coalescence. It is shown macro-channel subcooled boiling pressure drop and heat transfer correlations are unsuitable for micro-channel flows. However, two new modified correlations produced good predictions of the present heat transfer data.
机译:这项由两部分组成的研究的第二部分探讨了一种新的冷却方案的性能,在该方案中,流经微通道散热器的主要工作流体被制冷冷却系统间接冷却。本部分研究的目的是探讨散热器的压降和传热特性。在单相冷却期间,由于液体粘度降低,压降随热通量的增加而降低。但是,随着气泡离开后,随着热通量的增加,压降开始增加。这些相反的趋势使压降随热通量的变化最小。液体过冷度的增加降低了两相压降,这是由于气泡界面处的强凝结引起的空隙率降低以及气泡聚结的可能性降低。结果表明,大通道过冷沸腾压降和传热相关性不适用于微通道流动。但是,两个新的修改的相关性对当前的传热数据产生了良好的预测。

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