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Flow boiling heat transfer of Freon Rll and HCFCl23 in narrow passages

机译:氟利昂Rll和HCFCl23在狭窄通道中的流沸腾传热

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摘要

Flow boiling heat transfer coefficients for Freon Rll and HCFCl23 in a smooth copper tube with an inner diameter of 1.95 mm have been experimentally investigated. The parameter ranges examined are: heat fluxes from 5 to 200 kW m~-2; mass fluxes from 50 to l800 kg m~-2 s~-1; vapour quality from 0 to 0.9; system pressures from 200 to 500 kPa; and experimental heat transfer coefficients from l to l8 kW m~-2 K~-1. It was found that the heat transfer coefficients are a strong function of the heat flux and the system pressure, while the effects of mass flux and vapour quality are very small in the range examined. This suggests that the heat transfer is mainly via nucleate boiling. The present experimental data were compared with some existing correlations and recommendations on their use is made.
机译:实验研究了内径1.95 mm的光滑铜管中Freon Rll和HCFCl23的沸腾传热系数。检查的参数范围是:5至200 kW m〜-2的热通量;质量通量为50至l800 kg m〜-2 s〜-1;蒸气质量从0到0.9;系统压力为200至500 kPa;传热系数从l到l8 kW m〜-2 K〜-1。发现传热系数是热通量和系统压力的强函数,而质量通量和蒸气质量的影响在所研究的范围内很小。这表明传热主要是通过核沸腾进行的。将当前的实验数据与一些现有的相关性进行了比较,并提出了使用建议。

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