首页> 外文期刊>International Journal of Heat and Mass Transfer >CONDENSATION HEAT TRANSFER AND PRESSURE DROP OF REFRIGERANT R-134A IN A PLATE HEAT EXCHANGER
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CONDENSATION HEAT TRANSFER AND PRESSURE DROP OF REFRIGERANT R-134A IN A PLATE HEAT EXCHANGER

机译:板式换热器中制冷剂R-134A的冷凝传热和压降

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摘要

An experimental refrigerant loop has been established in the present study to measure the condensation heat transfer coefficient h_r and frictional pressure drop △P_f of R-134a in a vertical plate heat exchanger. Two vertical counter flow channels were formed in the exchanger by three plates of commercialized geometry with a corrugated sinusoidal shape of a chevron angle of 60 deg. Downflow of the condensing R-134a in one channel releases heat to the cold upflow of water in the other channel. The effects of the refrigerant mass flux, average imposed heat flux, system pressure(saturated temperature) and vapor quality of R-134a on the measured data were explored in detail. The results indicate that at a higher vapor quality the condensation heat transfer coefficient and pressure drop are significantly higher.
机译:在本研究中,已经建立了实验性制冷剂回路,以测量立式板式换热器中R-134a的冷凝传热系数h_r和摩擦压降△P_f。两个垂直的逆流通道由三块商业化的几何形状的板形成,这些板的波形呈正弦波状,人字形角度为60度。一个通道中冷凝的R-134a的向下流动将热量释放给另一通道中水的冷上升。详细探讨了R-134a的制冷剂质量通量,平均施加的热通量,系统压力(饱和温度)和蒸汽质量对测量数据的影响。结果表明,在较高的蒸气质量下,冷凝传热系数和压降明显更高。

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