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Analytical Modeling of Annular Flow Boiling Heat Transfer in Mini- and Microchannel Heat Sinks

机译:微型和微通道散热器中环形流沸腾换热的解析模型

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摘要

An analytical model is proposed to predict the flow boiling heat transfer coefficient in the annular flow regime in mini- and microchannel heat sinks based on the separated model. The modeling procedure includes a formulation for determining the heat transfer coefficient based on the wall shear stress and the local thermophysical characteristics of the fluid based on the Reynolds' analogy. The frictional and acceleration pressure gradients within the channel are incorporated into the present model to provide a better representation of the flow conditions. The model is validated against collected data sets from the literature produced by different authors under different experimental conditions, different fluids, and with mini- and microchannels of hydraulic diameters falling within the range of 92.1440 μm. The accuracy between the experimental and predicted results is achieved with a mean absolute error of 10%. The present analytical model can correctly predict the different trends of the heat transfer coefficient reported in the literature as a function of the exit quality. The predicted two-phase heat transfer coefficient is found to be very sensitive to changes in mass flux and saturation temperature. However, it is found to be mildly sensitive to the change in heat flux.
机译:提出了一种基于分离模型的微型和微通道散热器环形流动状态下沸腾传热系数的解析模型。建模过程包括一个公式,用于根据壁切应力和基于雷诺兹的类比确定流体的局部热物理特性来确定传热系数。通道内的摩擦压力梯度和加速压力梯度被合并到本模型中,以更好地表示流动状况。该模型针对不同作者在不同实验条件,不同流体以及水力直径的微型通道和微通道落在92.1440μm范围内的文献收集的数据集进行了验证。实验结果和预测结果之间的精度达到10%的平均绝对误差。本分析模型可以正确预测文献中报道的传热系数随出口质量变化的不同趋势。发现预测的两相传热系数对质量通量和饱和温度的变化非常敏感。但是,发现它对热通量的变化具有中等敏感性。

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