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FLOW BOILING HEAT TRANSFER OF R123/R134A MIXTURE IN A MICRO-CHANNEL

机译:R123 / R134A混合物在微通道中的沸腾传热

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This paper describes the flow boiling heat transfer of R123/R134a mixture in a single round micro-channel with 0.19 mm ID. The flow boiling heat transfer coefficients were measured with the variation of mixture composition (R123 mole fraction: 0.502, 0.746) at various experimental conditions: mass velocities (314, 392, 470 kg/m_(2)-s), heat fluxes (10, 15, 20 kW/m_(2)) and vapor qualities (0.2 - 0.85). The heat transfer characteristics of R123/R134a mixture are similar to those of pure R123 observed in the previous flow boiling experiment. The similarity of heat transfer characteristics denotes that the heat transfer is governed by evaporation of thin liquid film around the elongated bubbles like the case of pure R123. The heat transfer coefficients of R123/R134a mixture are compared with those of equivalent pure refrigerant by the correlation developed from pure R123 experimental results. The large reduction of heat transfer coefficients compared with pure refrigerant is found in micro-channels flow boiling by the mass transfer effect of mixed refrigerant. In addition, macro-channel correlations for mixed refrigerant do not make accurate prediction about the reduction of heat transfer coefficients.
机译:本文描述了在具有0.19 mm内径的单个圆形微通道中R123 / R134a混合物的流沸腾传热。在各种实验条件下测量沸腾沸腾的传热系数,其变化是混合物组成(R123摩尔分数:0.502,0.746):质量速度(314、392、470 kg / m_(2)-s),热通量(10) ,15、20 kW / m_(2))和蒸汽质量(0.2-0.85)。 R123 / R134a混合物的传热特性类似于在先前的沸腾实验中观察到的纯R123的传热特性。传热特性的相似性表明,与纯R123的情况一样,传热是由细长气泡周围的液态薄膜蒸发控制的。通过从纯R123实验结果得出的相关性,将R123 / R134a混合物的传热系数与等效纯制冷剂的传热系数进行了比较。通过混合制冷剂的传质作用,在微通道流沸腾中发现与纯制冷剂相比传热系数大大降低。另外,混合制冷剂的宏通道相关性不能对传热系数的降低做出准确的预测。

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