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Boiling heat transfer from a horizontal flat plate in a pool of liquid hydrogen

机译:在液氢池中从水平平板沸腾的传热

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Heat transfer from a flat plate facing upward immersed in a liquid hydrogen pool was measured for thepressures from atmospheric to 1.1 MPa. The flat plate heater used was 10 mm in width, 100 mm in lengthand 0.1 mm in thickness. Critical heat fluxes (CHFs) in saturated boiling increased with the increase inpressure up to around 0.3 MPa and then decreased with further pressure increase. The CHFs under sub-cooled condition at each pressure increased with the increase in sub-cooling. Discussions were made onthe experimental results by comparing with those of the other cryogenic liquids and also the Kutate-ladze's equations under saturated and subcooled conditions. The experimental CHFs were much smallerthan the Kutateladze's equation for higher pressure up to critical. The heater surface temperature wasfound to reach the critical temperature before the occurrence of hydrodynamic instability and jump tothe film boiling regime at the lower heat flux in the higher pressure range. It was suggested that the CHFsare determined not by the heat flux but by the temperature in the higher pressure range.
机译:测量从大气压下向上浸入液氢池的平板的传热,压力为大气压至1.1 MPa。所使用的平板加热器的宽度为10mm,长度为100mm,厚度为0.1mm。饱和沸腾中的临界热通量(CHFs)随着压力的升高而升高,直至约0.3 MPa,然后随着压力的进一步升高而降低。在每个压力下,过冷条件下的CHF随过冷量的增加而增加。通过与其他低温液体以及饱和和过冷条件下的Kutate-ladze方程进行比较,对实验结果进行了讨论。实验性CHF比Kutateladze方程小得多,后者可用于更高的临界压力。发现加热器表面温度在发生流体动力学不稳定之前已达到临界温度,并在较高压力范围内以较低热通量跃升至薄膜沸腾状态。建议CHF不是由热通量而是由较高压力范围内的温度决定。

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