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Comparison of condensation heat transfer and pressure drop of CO_2 in rectangular microchannels

机译:矩形微通道中凝结传热和CO_2压降的比较

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摘要

The in-tube condensation heat transfer characteristics of CO_2 in three different microchannels were investigated. The channels were rectangular, and the numbers of ports were 7,19, and 23. The hydraulic diameters were 1.5,0.78, and 0.68 mm for the 7,23, and 19 ports, respectively. The test temperature ranged from -5 to 5 ℃, and the range of the mass flux was from 400 to 800 kg/m~2 s. The condensation heat transfer coefficient increased with the decrease in hydraulic diameter, which is dominant at condensation temperatures of 0 and -5 ℃. Increasing and decreasing the heat transfer coefficient at critical vapor quality was observed for the microchannel of 23 ports. The highest pressure drop was found in the micro-channel of 23 ports too. The model by Thome et al. showed the smallest mean deviation of heat transfer coefficient, and the Mishima and Hibiki model had a mean deviation of ±30.1% for the frictional pressure drop.
机译:研究了三个不同微通道中CO_2的管内冷凝传热特性。通道为矩形,端口数分别为7,19和23。7,23和19个端口的液压直径分别为1.5、0.78和0.68 mm。试验温度为-5〜5℃,质量通量范围为400〜800kg / m〜2s。冷凝水的传热系数随水力直径的减小而增加,这在冷凝温度为0和-5℃时占主导地位。对于23个端口的微通道,观察到在临界蒸汽质量下传热系数的增大和减小。在23个端口的微通道中也发现了最高的压降。 Thome等人的模型。显示出最小的传热系数平均偏差,Mishima和Hibiki模型的摩擦压降平均偏差为±30.1%。

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