Flow Boiling Characteristics of R410A in Horizontal Annuli of Enhanced Surface Tubes

Zhi-chuan Sun, Wei Li, Xiang Ma, Yuansheng Lin, Z. Ke, H. Ke
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Abstract

An experimental study on the flow boiling heat transfer in a horizontal annular passage outside the single tube using R410A. The tested tubes contain a smooth tube, a 1EHT tube (dimpled tube) and a herringbone micro-fin tube with the same outside diameter of 12.70 mm. Tests were carried out at a saturation temperature of 6 °C for a mass flux range of 8∼107 kg/m2s with a fixed inlet quality of 0.1 and three different outlet qualities (0.4, 0.6, 0.8). Changes in vapor quality and annular gap size are found to have a significant impact on boiling heat transfer in the concentric annulus. For tests in the annuli with a 25.4-mm-ID outer tube, the HTC of the herringbone micro-fin tube is highest together with the largest pressure drop. Both the annulus of 1EHT tube and the annulus of herringbone micro-fin tube show a higher boiling HTC at an outlet quality of 0.6. The larger penalty factor is found at an outlet quality of 0.8. For flow boiling in the annuli having different annular gap sizes, it is found that the heat transfer enhancement ratio decreases sharply with the increasing average quality. When the inner diameter of outer tube is 19.0 mm, HTC decreases at first and then rises slowly. The huge bubbles occurred at the low mass fluxes and the scouring effect on the heated annulus walls of high-speed flow may be responsible.
R410A在强化表面管水平环空中的流动沸腾特性
利用R410A对单管外水平环形通道内流动沸腾换热进行了实验研究。测试管包括光滑管、1EHT管和人字微鳍管,外径相同,均为12.70 mm。试验在饱和温度6°C下进行,质量通量范围为8 ~ 107 kg/m2s,进口质量为固定0.1,出口质量为三种不同(0.4、0.6、0.8)。蒸汽质量和环空间隙大小的变化对同心环空沸腾换热有显著影响。在外管直径为25.4 mm的环空中,人字微鳍管的HTC最高,压降最大。在出口质量为0.6时,1EHT管环空和人字微翅管环空均表现出较高的沸腾HTC。出口质量为0.8时,惩罚因子较大。对于不同环隙大小的环空流动沸腾,传热强化比随着平均质量的增大而急剧减小。当外管内径为19.0 mm时,HTC先下降后缓慢上升。在低质量通量下产生的巨大气泡和高速流动对加热环空壁面的冲刷效应可能是主要原因。
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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