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Flow boiling heat transfer of R407C in a microchannels based heat spreader

机译:基于微通道的散热器中R407C的流沸腾传热

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摘要

New flow boiling experimental results for R407C in a microchannel based heat spreader are presented. Boiling curves were obtained for heat fluxes up to 310 kW/m~2 (based on the footprint area), mass velocities from 400 to 1500 kg/m~2s, liquid subcoolings at the test section inlet of 5, 10 and 15 °C and saturation temperatures referred to the pressure at the heat sink inlet of approximately 25 °C. Based on these results, heat sink averaged heat transfer coefficients during convective boiling were estimated. The heat sink evaluated in the present study is comprised of fifty parallel rectangular channels with cross-section dimensions of 100 × 500 lm, and total length of 15 mm. Average heat transfer coefficients up to 30 kW/m~2 °C were obtained. It was also found that the boiling curve moves to the left hand side with decreasing the mass velocity and liquid subcooling at the heat-sink inlet. Moreover, for a fixed heat-sink averaged vapor quality, the average heat transfer coefficient increases with increasing mass velocity. Under similar experimental conditions, the refrigerant R134a provided higher heat transfer coefficients than R407C. Additionally, during flow boiling of R407C, pressure oscillations with lower amplitude and frequency were observed compared to R134a. No one of the heat transfer predictive methods evaluated in the present study was accurate enough to predict the present R407C database.
机译:提出了基于微通道散热器的R407C的新沸腾实验结果。对于最高310 kW / m〜2(基于占地面积)的热通量,从400到1500 kg / m〜2s的质量速度,在5、10和15°C的测试段入口处的液体过冷情况,获得沸腾曲线饱和温度是指散热器入口处大约25°C的压力。根据这些结果,可以估算对流沸腾过程中的散热器平均传热系数。在本研究中评估的散热器由五十个平行的矩形通道组成,这些通道的横截面尺寸为100×500 lm,总长度为15 mm。获得了高达30 kW / m〜2°C的平均传热系数。还发现沸腾曲线向左移动,同时降低了质量速度和散热器入口处的液体过冷。此外,对于固定的散热器平均蒸汽质量,平均传热系数随质量速度的增加而增加。在相似的实验条件下,制冷剂R134a提供的传热系数高于R407C。另外,在R407C的沸腾过程中,与R134a相比,观察到振幅和频率较低的压力振荡。在本研究中评估的传热预测方法中,没有一种能够足够准确地预测当前的R407C数据库。

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