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EXPERIMENTAL STUDY ON CONDENSATION IN THE OUTER ANNULAR REGION OUTSIDE HORIZONTAL ENHANCED TUBES

机译:水平增强管外环区域冷凝的实验研究

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Single-phase and flow condensation experiments were performed using refrigerant R410A in the outer annular region of horizontal enhanced tube with different enhanced surfaces at a saturation temperature of 45°C in the range of mass flux 44.43-102.23kg/(m~2s). The vapor quality ranges from 0.8 to 0.2. The outer diameters of the tubes are all 19.05mm. but the inner diameters are slightly different due to different surface structures. The surface structures of the three enhanced tubes are fins(EHTl tube), toothed structures (EHT2 tube) and fine cavities(EHT3 tube) of different sizes and densities. Among them, the EHT3 tube has internal threads. Wilson diagram method was used to determine the enhancement ratio of the water side heat transfer coefficient of EHT3 tube. It was found that the pressure drop increased with the increase of mass flux, while the heat transfer coefficient showed different trends, and the smooth tube was always the lowest of the four tubes. A comprehensive evaluation factor α combining heat transfer enhancement factor(EF) and pressure drop penalty factor(PF) was defined, in which EHT2 tube (1.38-1.75) was the largest, with strong heat transfer capacity and small pressure drop, so the condensing heat transfer capacity of EMT2 tube was the best.
机译:使用水平增强管的外环形区域中的制冷剂R410a进行单相和流动缩合实验,在质量磁通范围内的45℃的饱和度温度下具有不同的增强表面,在质量通量44.43-102.23kg /(m〜2s)的范围内。蒸汽质量范围为0.8至0.2。管的外径全部为19.05mm。但由于不同的表面结构,内径略有不同。三个增强管的表面结构是翅片(EHTL管),齿形结构(EHT2管)和不同尺寸和密度的细腔(EHT3管)。其中,EHT3管具有内线。威尔逊图方法用于确定EHT3管的水侧传热系数的增强比。结果发现,随着质量磁通量的增加,压降随着质量磁通量的增加而增加,而传热系数显示出不同的趋势,并且光滑管始终是四管中最低的。定义了综合评价因子α组合传热增强因子(EF)和压降惩罚因子(PF),其中EHT2管(1.38-1.75)是最大的,具有强大的传热能力和小的压降,所以冷凝EMT2管的传热能力是最好的。

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