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首页> 外文期刊>International Journal of Multiphase Flow >Flow boiling heat transfer coefficients and pressure drop of FC-72 in microchannels
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Flow boiling heat transfer coefficients and pressure drop of FC-72 in microchannels

机译:FC-72在微通道中的沸腾传热系数和压降

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摘要

The two-phase pressure drop and heat transfer coefficients of FC-72(C _6F _(14)) in two multi-ported rectangular microchannels with hydraulic diameters of 61 and 278μm were measured by varying heat flux from 0.6 to 45.1kW/m ~2 and mass flux from 188 to 1539kg/m ~2s. Direct heating using a DC power supply provided a heating load to the test section. The pressure drop increased with increasing vapor quality and mass flux. The heat flux negligibly affected the pressure drop under identical mass flux and vapor quality conditions, indicating that most of the pressure drop was caused by friction. When the vapor quality exceeded 0.2-0.4, the heat transfer coefficient decreased with increasing vapor quality due to early dry-out of liquid film on the channel surface. In addition, the comparison between the predicted pressure drop and heat transfer coefficient by the existing correlations and the measured values was presented.
机译:通过从0.6到45.1kW / m的热通量测量两个水力直径分别为61和278μm的矩形矩形多通道矩形通道中FC-72(C _6F _(14))的两相压降和传热系数2和质量通量从188到1539kg / m〜2s。使用直流电源直接加热为测试部分提供了加热负载。压降随着蒸汽质量和质量通量的增加而增加。在相同的质量通量和蒸汽质量条件下,热通量对压降的影响可忽略不计,表明大部分压降是由摩擦引起的。当蒸气质量超过0.2-0.4时,由于通道表面上液膜的早期变干,传热系数随着蒸气质量的增加而降低。另外,通过现有的相关性和测量值对预测的压降和传热系数进行了比较。

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