高温脉动热管的传热特性及传热极限可视化实验研究

Visualization Experiment Study on Heat Transfer Characteristic and Limit of High-temperature Oscillating Heat Pipe

  • 摘要: 高温脉动热管由于其高效传热能力及结构简单等特点在核能领域等高温环境下的高热流疏导领域有着广阔的应用前景。为了对高温脉动热管的传热特性及传热极限进行深入分析,搭建了高温脉动热管可视化实验台,通过X射线成像技术,首次实现了以铯为工质的单弯头高温脉动热管工作状态及传热极限状态的可视化,并结合壁面温度场分析了传热特性,探究了随着加热功率增大脉动热管的性能变化以及流动状态的转变。结果表明,随着加热功率增大工质由脉动转变为单向流动,热阻由250 W时的1.62 ℃/W减小至400 W的0.84 ℃/W,并在450 W达到传热极限。传热极限初期液态工质于绝热段及冷凝段之间脉动,最终堆积在冷凝段无法回流,但仍有液膜沿管壁向下流动。

     

    Abstract: The high-temperature oscillating heat pipe (HTOHP) has broad application prospects in the field of high heat flux dissipation in high-temperature environments such as nuclear energy and aerospace because of its efficient heat transfer capability and simple structure. To conduct an in-depth analysis of the heat transfer characteristics and heat transfer limit of the HTOHP, a visualization experiment setup was constructed. By utilizing X-ray imaging technology, the working and heat transfer limit states of a single-turn HTOHP with cesium as the working fluid were visualized. Additionally, an analysis of the wall temperature field was conducted to explore the thermal performance changes and flow state transitions of the HTOHP as the heating power increased. The results indicate that the thermal resistance decreases from 1.62 ℃/W at 250 W to 0.84 ℃/W at 400 W, and rapidly increases after reaching the heat transfer limit at 450 W. This phenomenon is primarily due to the transition of the working fluid from an oscillating flow state to unidirectional flow state as the heating power increases. When reaching the heat transfer limit, the working fluid stopovers and then accumulates in the condensation section of the HTOHP, preventing return flow, although a liquid film still flows down along the tube wall. When the HTOHP starts up and at a low heating power of 250 W, a phenomenon is observed where the unidirectional flow state cannot be sustained. This is because under low heating power conditions, after entering unidirectional circulation, the heat transfer efficiency of the HTOHP is improved, causing a decrease in the temperature of the evaporation section. This results in a reduced phase change heat transfer rate, which is insufficient to maintain unidirectional flow. At the limit power, due to the working fluid of the HTOHP being in unidirectional flow and unable to form a more optimal flow state, the heat from the evaporation section cannot be fully dissipated, leading to a continuous increase in the evaporator section temperature. When the evaporator section temperature reaches 656.71 ℃, due to the excessive rate of evaporative heat transfer, a stopover phenomenon occurs under the influence of working fluid pressure, ultimately resulting in the heat transfer limit being reached. It is worth noting that at the heat transfer limit state, there is still a liquid film adhering to the wall and flowing downward. Consequently, the adiabatic and evaporation sections of the HTOHP are not filled with gas. Therefore, the limit state does not exist in a manner where the pipe conducts heat solely as an empty tube.

     

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