Augmented Performance of Flow Boiling Heat Transfer in a Tube With Axial Micro-Grooves and its Augmentation Mechanisms

Lixin Cheng, Tingkuan Chen
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Abstract

Experiments of upward flow boiling heat transfer with water in a vertical smooth tube and a tube with axial micro-grooves were respectively conducted. Both of the tested tubes have a length of 2.5 m, an inner diameter of 15 mm and an outlet diameter of 19 mm. The tube with axial micro grooves has many micro rectangle grooves in its inner wall along the axial direction. The grooves have a depth of 0.5 mm and a width of 0.3 mm. The tests were performed at an absolute pressure of 6 bar. The heat flux ranged from 0 to 550 kW/m2 and the mass flux was selected at 410, 610 and 810 kg/m2s, respectively. By comparison, flow boiling heat transfer coefficients in the enhanced tube are 1.6 ∼ 2.7 fold that in the smooth tube while the frictional pressure drop in the enhanced tube is slightly greater than that in the smooth tube. The augmentation of flow boiling heat transfer in the tube with axial micro-grooves is apparent. Based on the experimental data, a correlation of flow boiling heat transfer is proposed for the enhanced tube. Finally, the mechanisms of heat transfer enhancement are analyzed.
轴向微槽管内流动沸腾换热的增强性能及其增强机理
分别在竖直光滑管和轴向微槽管内进行了水向上流动沸腾换热实验。两个测试管的长度为2.5 m,内径为15 mm,出口直径为19 mm。轴向微槽管的内壁沿轴向有许多矩形微槽。所述凹槽深度为0.5 mm,宽度为0.3 mm。试验在6巴的绝对压力下进行。热流密度为0 ~ 550 kW/m2,质量流密度分别为410、610和810 kg/m2s。相比之下,强化管的流动沸腾换热系数是光滑管的1.6 ~ 2.7倍,而摩擦压降略大于光滑管。轴向微槽对管内流动沸腾换热有明显的增强作用。在实验数据的基础上,提出了强化管流动沸腾传热的关系式。最后,分析了强化传热的机理。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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