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Flow Boiling Heat Transfer in MicroChannels

机译:微通道中的流沸腾传热

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Flow boiling heat transfer to water in microchannels is experimentally investigated. The dimensions of the microchannels considered are 275 × 636 and 406 × 1063 μm~2. The experiments are conducted at inlet water temperatures in the range of 67-95 ℃ and mass fluxes of 221-1283 kg/m~2 s. The maximum heat flux investigated in the tests is 129 W/cm~2 and the maximum exit quality is 0.2. Convective boiling heat transfer coefficients are measured and compared to predictions from existing correlations for larger channels. While an existing correlation was found to provide satisfactory prediction of the heat transfer coefficient in subcooled boiling in microchannels, saturated boiling was not well predicted by the correlations for macrochannels. A new superposition model is developed to correlate the heat transfer data in the saturated boiling regime in micro-channel flows. In this model, specific features of flow boiling in microchannels are incorporated while deriving analytical solutions for the convection enhancement factor and nucleate boiling suppression factor. Good agreement with the experimental measurements indicates that this model is suitable for use in analyzing boiling heat transfer in micro-channel flows.
机译:实验研究了流沸腾传热到微通道中的水。所考虑的微通道的尺寸为275×636和406×1063μm〜2。实验是在进水温度为67-95℃,质量通量为221-1283 kg / m〜2 s的条件下进行的。试验中研究的最大热通量为129 W / cm〜2,最大出口质量为0.2。测量对流沸腾传热系数,并将其与较大通道现有相关性的预测值进行比较。虽然发现现有的相关性可以令人满意地预测微通道中过冷沸腾的传热系数,但是通过大通道的相关性并不能很好地预测饱和沸腾。开发了一种新的叠加模型,以关联微通道流中饱和沸腾状态下的传热数据。在该模型中,结合了微通道中沸腾的特定特征,同时得出了对流增强因子和成核沸腾抑制因子的解析解。与实验测量结果吻合良好,表明该模型适用于分析微通道流中的沸腾传热。

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