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首页> 外文期刊>International communications in heat and mass transfer >Solution of the boundary-layer equations for natural convection film boiling on vertical cylindrical surfaces
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Solution of the boundary-layer equations for natural convection film boiling on vertical cylindrical surfaces

机译:垂直圆柱表面上自然对流膜沸腾的边界层方程解

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摘要

Film boiling around a cylinder has been studied with a pseudo-similarity method. The velocity, temperature profile, the heat and mass transfer performance and the vapor film thickness could be predicted by the model with the effects of thermal properties (Pr, vapor liquid pμ ratio, and cpv(T_w-T_(sat))/(h_(lv)Pr)) considered. The results show that the heat transfer performance of film boiling on a cylinder surface is much higher than that on a flat surface. The film temperature and the Nusselt number of the numerical model agree well with the experimental data from the literature within the tested ranges. The heat transfer rate and local heat flux of the pseudo-similarity method in this work are also compared with that of the perturbation method, the results from those two method are found a perfect match.
机译:已经用伪相似方法研究了汽缸周围的薄膜沸腾。该模型可以通过热特性(Pr,气液pμ比和cpv(T_w-T_(sat))/(h_)的影响来预测速度,温度分布,传热和传质性能以及蒸气膜厚度。 (lv)Pr))考虑。结果表明,在圆柱表面上沸腾的薄膜的传热性能远比在平面上沸腾的传热性能高。在测试范围内,薄膜温度和数值模型的努塞尔数与文献的实验数据吻合良好。将伪相似方法的传热速率和局部热通量与摄动方法的传热速率和局部热通量进行了比较,发现这两种方法的结果是完美匹配。

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