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An Experimental Investigation on the Flow Instability in Evaporator of Separate Type Heat Pipe

机译:单独式热管蒸发器流动不稳定的实验研究

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Because of the significance of engineering applications and arisen problems in the small inclination angle evaporator or horizontal evaporator of Separate Type Heat Pipe (STHP), an experimental investigation on the working fluid flow characteristics and the flow instability in the evaporator was presented. Flow patterns were observed and analyzed by visualization experiment. It was found that bubble flow, slug flow, wave foam flow occurred orderly in the evaporator with a small inclination angle when the heat flux increased, but the annular flow was not found, which appeared in a vertical evaporator. Two types of flow instabilities occurred, they were the flow pattern transformation instability and the density wave instability. The effects of pressure, mass velocity, inlet subcooling, heat flux, exit throttle on the flow instability were determined in the modelling experiment. The thresholds of the flow pattern transformation instability and that of the density wave instability were obtained. Nondimensional correlations for predicting the flow instability in STHP were given by means of one-dimension single-fluid model. The results may be used for the engineering design of large scale heat exchangers of STHP with a small inclination angle in evaporator.
机译:由于工程应用的重要性和在单独的型热管(STHP)的小倾角蒸发器或水平蒸发器中出现的问题,提出了对蒸发器中的工作流体流动特性和流动不稳定性的实验研究。通过可视化实验观察和分析流动模式。结果发现,当热通量增加时,蒸发器在蒸发器中有较小的倾斜角度出现的蒸发器中的蒸发器中出现的泡沫流动,但是未发现环形流动,这在垂直蒸发器中出现了环形流动。发生了两种类型的流动不稳定性,它们是流动模式变换不稳定和密度波不稳定性。在建模实验中确定了压力,质量速度,入口过冷,热通量,输出节流阀在流动不稳定性上的影响。获得了流动模式变换不稳定性的阈值以及密度波不稳定性的阈值。通过单尺寸单流体模型给出了预测STHP中流动不稳定性的非统计相关性。结果可用于蒸发器中具有小倾斜角的STHP大型热交换器的工程设计。

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