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HIGH HEAT FLUX SUBCOOLED FLOW BOILING OF METHANOL IN MICROTUBES

机译:微管中甲醇的高热通量过冷沸腾

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摘要

As the proper cooling of the electronic devices leads to significant increase in the performance, two-phase heat transfer to dielectric liquids can be of an interest especially for thermal management solutions for high power density devices with extremely high heat fluxes. In this paper, the pressure drop and critical heat flux (CHF) for subcooled flow boiling of methanol at high heat fluxes exceeding 1 kW/cm~2 is investigated. Methanol was propelled into microtubes (ID= 265 and 150 μm) at flow rates up to 40 ml/min (mass fluxes approaching 10000 kg/m~2-s), boiled in a portion of the microtube by passing DC current through the walls, and the two-phase pressure drop and CHF were measured for a range of operating parameters. The two-phase pressure drop for subcooled flow boiling was found to be significantly lower than the saturated flow boiling case, which can lead to lower pumping powers and more stability in the cooling systems. CHF was found to be increasing almost linearly with Re and inverse of inner diameter (I/ID), while for a given inner diameter, it decreases with increasing heated length.
机译:由于电子设备的适当冷却会导致性能显着提高,因此特别需要用于热通量极高的高功率密度设备的热管理解决方案时,向介电液体的两相传热可能会引起人们的关注。本文研究了在超过1 kW / cm〜2的高热通量下甲醇过冷沸腾的压降和临界热通量(CHF)。以高达40 ml / min(质量通量接近10000 kg / m〜2-s)的流速将甲醇推进微管(ID = 265和150μm)中,通过使直流电流通过壁将其煮沸在微管的一部分中,并针对一系列操作参数测量了两相压降和CHF。发现过冷流沸腾的两相压降明显低于饱和流沸腾的情况,这可能导致较低的泵送功率和冷却​​系统的更高稳定性。发现CHF随Re和内径(I / ID)的倒数几乎呈线性增加,而对于给定的内径,CHF随加热长度的增加而减小。

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