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Analytical and experimental investigations on heat transport capability of axially grooved aluminium-methane heat pipe

机译:轴向槽铝 - 甲烷热管热传输能力的分析与实验研究

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摘要

An analytical model for predicting heat transport capability of an axially grooved aluminium-methane heat pipe is presented, considering the effect of liquid-vapour interfacial shear stress and the axial variation of the liquid-vapour interfacial radius. The effects of undercharge and overcharge of the working fluid on the performance of the heat pipe are studied for the operating temperatures below and above a nominal operating temperature, respectively. In order to validate the model results, an axially grooved aluminium-methane heat pipe was fabricated and tested for its heat transport capability between 100 K and 160 K at horizontal tilt and an adverse tilt of 2.5 mm. It was observed that during heat pipe dry out, in addition to the evaporator temperature rise, there is a rapid fall in the condenser temperature due to cessation of fluid flow. Model results are found to be in reasonably good agreement with the experimental results till the nominal temperature of 130 K for both horizontal and adverse tilts. Beyond 130 K, the experimental heat transport capabilities at horizontal tilt are much more than the prediction which could possibly be due to the conductive and convective heat transfer through the puddle and the evaporative heat transfer through the thin film of the corners of the puddle extending into the evaporator. Beyond 130 K, the experimental heat transport capabilities at adverse tilt are also much more than the prediction which could possibly be due to the heat leak into the puddle entering into the adiabatic zone.
机译:提出了一种用于预测轴向槽铝 - 甲烷热管的热传递能力的分析模型,考虑到液态蒸汽界面剪切应力和液态蒸汽界面半径的轴向变化的效果。研究了工作流体对热管性能的充电和过充电的影响,分别用于低于标称工作温度的工作温度。为了验证模型结果,制造轴向槽的铝 - 甲烷热管,并在横向倾斜的横向倾斜度和160 k之间进行热传递能力,并且不良倾斜为2.5mm。观察到,在热管干燥期间,除了蒸发器温度上升之外,由于流体流动的停止,在冷凝器温度下存在快速下降。发现模型结果与实验结果相当好,直到水平和不利倾斜的标称温度为130 k。超过130 k,水平倾斜的实验热传输能力远远大于预测,这可能是由于通过水坑的导电和对流传热和通过延伸进入的水坑的薄膜的薄膜的导电和对流热传递而导致的预测蒸发器。超过130 k,不利倾斜的实验热传输能力也远远超过预测,这可能是由于进入绝热区的水坑中的热量。

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