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Flow boiling heat transfer in two-phase micro-channel heat sinks―Ⅰ. Experimental investigation and assessment of correlation methods

机译:两相微通道散热器的流沸腾换热Ⅰ。相关方法的实验研究与评估

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This paper is the first of a two-part study concerning measurement and prediction of saturated flow boiling heat transfer in a water-cooled micro-channel heat sink. In this paper, new experimental results are discussed which provide new physical insight into the unique nature of flow boiling in narrow rectangular micro-channels. The micro-channel heat sink contained 21 parallel channels having a 231 x 713μm cross-section. Tests were performed with deionized water over a mass velocity range of 135-402 kg/m~2 s, inlet temperatures of 30 and 60℃, and an outlet pressure of 1.17 bar. Results indicate an abrupt transition to annular flow near the point of zero thermodynamic equilibrium quality, and reveal the dominant heat transfer mechanism is forced convective boiling corresponding to annular flow. Contrary to macro-channel trends, the heat transfer coefficient is shown to decrease with increasing thermodynamic equilibrium quality. This unique trend is attributed to appreciable droplet entrainment at the onset of annular flow regime development, and the increase in mass flow rate of the annular film by droplet deposition downstream. Eleven previous empirical correlations are assessed and deemed unable to predict the correct trend of heat transfer coefficient with quality because of the unique nature of flow boiling in micro-channels, and the operating conditions of water-cooled micro-channel heat sinks falling outside the recommended application range for most correlations. Part II of this study will introduce a new annular flow model as an alternative approach to heat transfer coefficient prediction for micro-channels.
机译:本文是由两部分组成的研究的第一部分,该研究涉及水冷微通道散热器中饱和流沸腾传热的测量和预测。在本文中,讨论了新的实验结果,这些新结果提供了对窄矩形微通道中流动沸腾的独特性质的新物理见解。微通道散热器包含21个平行通道,其横截面为231 x713μm。用去离子水在135-402 kg / m〜2 s的质量速度范围内,入口温度为30和60℃,出口压力为1.17 bar的条件下进行测试。结果表明,在热力学平衡质量为零的点附近突然转变为环形流动,并揭示了主要的传热机制是与环形流动相对应的强迫对流沸腾。与大通道趋势相反,传热系数显示出随着热力学平衡质量的增加而降低。这种独特的趋势归因于在环形流态发展开始时明显的液滴夹带,以及由于下游的液滴沉积而导致的环形膜的质量流率的增加。由于微通道中的流动沸腾具有独特的性质,并且水冷式微通道散热器的工作条件不在推荐范围之内,因此评估了11种先前的经验相关性,并认为它们无法以质量预测正确的传热系数趋势。大多数相关性的应用范围。本研究的第二部分将介绍一种新的环形流动模型,作为预测微通道传热系数的替代方法。

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