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Effect Of Void Fraction Models On The Film Thickness Of R134a During Downward Condensation In A Vertical Smooth Tube

机译:垂直分流管中空隙率模型对R134a膜向下冷凝过程中膜厚的影响

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In the present study, the void fraction and film thickness of pure R-134a flowing downwards in a vertical condenser tube are indirectly determined using relevant measured data together with an annular flow model and various void fraction models reported in the open literature. The vertical test section is a countercurrent flow double tube heat exchanger with refrigerant flowing down in the inner tube and cooling water flowing upward in the annulus. The inner tube is made from smooth copper tubing of 9.52 mm outer diameter with a length of 0.5 m. The experimental runs are carried out at average saturated condensing temperatures of 40 and 50 ℃, and mass velocities are around 456 kg m~(-2) s~(-1), over the vapour quality range 0.82-0.93, while the heat fluxes are between 45.60 and 50.90 kW m~(-2). Analysis based on simple void fraction models of the annular flow pattern are presented for forced convection condensation of pure R134a, taking into account the effect of the different saturation temperatures at high mass flux conditions. The comparisons of calculated film thickness show that the void fraction models of Spedding and Chen, and Chisholm and Armand are the most accurate ones with the experimental data due to their low deviation with Whalley's annular flow model over 35 void fraction models presented in this paper.
机译:在本研究中,在垂直冷凝器管中向下流动的纯R-134a的空隙率和膜厚是使用相关的测量数据以及环形流动模型和公开文献中报道的各种空隙率模型间接确定的。垂直测试部分是一个逆流双管热交换器,制冷剂在内管中向下流动,冷却水在环空中向上流动。内管由外径为9.52 mm,长度为0.5 m的光滑铜管制成。在40和50℃的平均饱和冷凝温度下进行实验,在蒸汽质量范围为0.82-0.93的范围内,质量速度约为456 kg m〜(-2)s〜(-1)。在45.60至50.90 kW m〜(-2)之间考虑到在高质量通量条件下不同饱和温度的影响,提出了基于简单的环形流型空隙率模型的分析,用于纯R134a的强制对流冷凝。计算出的薄膜厚度的比较表明,由于Spedding和Chen,Chisholm和Armand的空隙率模型与Whalley环形流模型相比在本文提出的35个空隙率模型中偏差较小,因此它们是最准确的实验数据。

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