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NUMERICAL INVESTIGATION ON SATURATED BOILING HEAT TRANSFER IN A VERTICAL RECTANGULAR MINICHANNEL

机译:垂直矩形百分之烷基中饱和沸热传热的数值研究

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A numerical method based on the Euler-Euler model was developed to investigate the mechanism of saturated boiling heat transfer mechanism on upward flow in a vertical rectangular minichannel. This method validated by the experimental data from literature. At the same time, the mechanism of saturated boiling heat transfer was also investigated by ANSYS CFX for Freon R21 at high vapor quality in a vertical rectangular minichannel based on the above numerical method. The results show that the simulation results are good agreement with experimental data from reference and the deviation is within ±15%. The main boiling mechanism is forced convective boiling while the contribution of nucleate boiling is slight for saturated boiling heat transfer at high vapor quality. The evaporation of dispersed liquid phase should be also a main boiling heat transfer mechanism. These results will provide some constructive instructions for the understanding of saturated boiling heat transfer phenomenon in a vertical rectangular minichannel of PFHE.
机译:开发了一种基于Euler-euler模型的数值方法,以研究饱和沸腾传热机制在垂直矩形百分之烷基中的向上流动的机理。该方法由文献的实验数据验证。同时,基于上述数值方法,在垂直矩形迷你群中的高蒸汽质量下,还通过ANSYS CFX来研究饱和沸腾热传递的机制。结果表明,仿真结果与来自参考的实验数据吻合良好,偏差在±15%范围内。主要沸腾机构是强迫对流沸腾的,而核心沸腾的贡献是在高蒸气质量下饱和沸腾的热传递的贡献。分散液相的蒸发应该是主要沸腾的传热机制。这些结果将提供一些建设性指示,以了解PfHe垂直矩形百分之千烷基中的饱和沸腾传热现象。

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