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Flow Boiling Heat Transfer Characteristics of R32 inside a Horizontal Small-diameter Microfin Tube

机译:水平小直径微素管内R32的流沸热特性

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This study experimentally investigated the flow boiling heat transfer and pressure drop characteristics of refrigerant R32 in a horizontal small-diameter microfin tube that had an outer diameter of 3.0 mm and an equivalent diameter of 2.6 mm. The test microfin tube had a helix angle of 10°, a fin height of 0.1 mm, and 25 fins. The flow boiling heat transfer coefficient and the pressure drop were measured against a mass velocities range of 100-400 kg/(m~2s), a heat flux range of 5-20 kW/m~2, and a saturation temperature of 15°C. The heat transfer coefficient was found to increase with an increase in the heat flux and the vapor quality in the pre-dryout region. The effect of tube diameter on heat transfer in small-diameter microfin tubes - tubes with equivalent diameters of 2.6 mm and 3.7 mm - that had the same number and height of fins, is significant in the forced convection and thin liquid film evaporation heat transfer dominant regions compared to the nucleate boiling dominant region.
机译:本研究通过外径为3.0mm的水平小直径微素管中的制冷剂R32的流动沸腾热传递和压力下降特性,其外径为3.0mm,等效直径为2.6mm。测试微素管的螺旋角为10°,翅片高度为0.1mm,25个翅片。测量流动沸腾的传热系数和压降抵抗100-400kg /(m〜2s)的质量速度,热通量范围为5-20 kW / m〜2,饱和温度为15° C。发现传热系数随着在干扰区域中的热通量和蒸汽质量的增加而增加。管直径对具有相同数量和3.7mm的小直径微素管 - 管中的热传递的影响 - 具有相同数量和高度的翅片,在强制对流和薄液膜蒸发热传递中显着与核心沸腾的主导地区相比的区域。

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