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扁管微小通道内R134a的沸腾换热试验

詹宏波 文涛 张大林

詹宏波, 文涛, 张大林. 扁管微小通道内R134a的沸腾换热试验[J]. 航空动力学报, 2017, 32(7): 1585-1591. doi: 10.13224/j.cnki.jasp.2017.07.007
引用本文: 詹宏波, 文涛, 张大林. 扁管微小通道内R134a的沸腾换热试验[J]. 航空动力学报, 2017, 32(7): 1585-1591. doi: 10.13224/j.cnki.jasp.2017.07.007
Experiment on flow boiling heat transfer of R134a in mini-channel of flat tube[J]. Journal of Aerospace Power, 2017, 32(7): 1585-1591. doi: 10.13224/j.cnki.jasp.2017.07.007
Citation: Experiment on flow boiling heat transfer of R134a in mini-channel of flat tube[J]. Journal of Aerospace Power, 2017, 32(7): 1585-1591. doi: 10.13224/j.cnki.jasp.2017.07.007

扁管微小通道内R134a的沸腾换热试验

doi: 10.13224/j.cnki.jasp.2017.07.007

Experiment on flow boiling heat transfer of R134a in mini-channel of flat tube

  • 摘要: 搭建适用于多种结构微小通道的沸腾换热试验系统,研究了制冷剂R134a在当量直径分别为0.63mm和0.72mm的多孔扁管微小通道内的沸腾换热特性。试验参数包括制冷剂质量流率为82~621kg/(m2·s),饱和压力为0.22~0.63MPa,干度为0~1;采用等热流密度方式加热,热流密度范围为9.7~64kW/m2。结果表明:R134a在扁管内沸腾换热中,当干度在0~0.6区间时,微小通道的传热系数明显高于常规通道,换热类型主要为核态沸腾,传热系数随热流密度和饱和压力的增大而增大,与质量流率关系不大;当干度大于0.6之后,传热系数随着干度的增大急剧减小,且在此干度区间,传热系数受热流密度和饱和压力影响较小,而受质量流率的影响相对较大。利用该结论和公开文献中R134a沸腾换热试验数据对Gungor-Winterton公式进行改进,改进后的公式对所有试验点的平均相对误差为-1.17%,平均绝对误差为19.24%,预测精度有了明显提高。

     

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出版历程
  • 收稿日期:  2015-10-25
  • 刊出日期:  2017-07-28

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