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Numerical Study on Condensation Heat and Mass Transfer of Refrigerants on a Vertical Channel in Presence of a Non-Condensable Gas

机译:存在不凝性气体时垂直通道上制冷剂冷凝传热传质的数值研究

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摘要

The purpose of this study is to analyse the combined heat and the mass transfer of liquid film condensation of vapour-gas mixtures (refrigerants R113 and R134a) in the presence of non-condensable gas (air) inside a vertical channel. Both liquid and gas mixtures are approached by two coupled laminar boundary layer. An implicit finite difference method is employed to solve the coupled governing equations for liquid film and gas flow together with the interfacial matching conditions. The effects of a wide range of changes of two independent variables (inlet Reynolds number and the inlet-to-wall temperature difference) on the local Nusselt number, accumulated condensate rate and dimensionless mass fraction at an exit channel are carefully examined. The numerical results indicate that the condensation of refrigerant R113 is important in comparison with the refrigerant R134a at higher difference temperature and lower speed of vapour-air, and the presence of non-condensable gas was found to have a weak effect on the refrigerant Rl 13 relative to R134a.
机译:这项研究的目的是分析在垂直通道内存在不可冷凝气体(空气)的情况下,蒸汽-气体混合物(制冷剂R113和R134a)的液膜冷凝的综合热量和传质。液体和气体混合物都通过两个耦合的层流边界层接近。采用隐式有限差分法求解液膜和气体的耦合控制方程及界面匹配条件。仔细检查了两个独立变量(入口雷诺数和入口至壁温差)的大范围变化对局部Nusselt数,出口通道处的累积冷凝率和无量纲质量分数的影响。数值结果表明,在较高的温度差和较低的蒸气速度下,与制冷剂R134a相比,制冷剂R113的冷凝是重要的,并且发现不可冷凝气体的存在对制冷剂Rl 13的影响较弱。相对于R134a。

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