首页> 外文会议>International Conference on Microchannels and Minichannels(ICMM2004); 20040617-20040619; Rochester,NY; US >EXPERIMENTAL STUDY OF HEAT TRANSFER, PRESSURE DROP, AND DRYOUT FOR FLOW BOILING OF WATER IN AN OIL HEATED MINICHANNEL
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EXPERIMENTAL STUDY OF HEAT TRANSFER, PRESSURE DROP, AND DRYOUT FOR FLOW BOILING OF WATER IN AN OIL HEATED MINICHANNEL

机译:油加热微型通道中水流沸腾的传热,压降和干燥的实验研究

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摘要

Heat transfer and pressure drop, are experimentally recorded for flow boiling water in a single 706 μm circular copper channel 158.75 mm long. Heat is supplied by heat transfer oil at specified temperatures to a helical channel in the test section. In contrast to other current experimental techniques for flow boiling in small diameter tubes, a uniform temperature boundary condition is employed rather than a constant heat flux condition. The principal results of these experiments are two-phase flow boiling heat transfer rates and an analysis of the time-dependent pressure drop signature during two-phase flow in a minichannel. The range of experiments includes mass fluxes of 43.8-3070 kg/m~2 s and wall temperatures of 100℃-171.2℃. In all cases the test section water inlet is subcooled to between 72.9℃ and 99.6℃. The inlet pressures used are 1.1-230.5 kPa (gage).
机译:实验记录了单个706μm长158.75 mm的圆形铜通道中流动沸腾水的传热和压降。导热油在规定的温度下将热量提供给测试部分的螺旋通道。与其他当前在小直径管中进行沸腾沸腾的实验技术相反,采用均匀的温度边界条件而不是恒定的热通量条件。这些实验的主要结果是两相流沸腾传热速率以及在微通道中两相流过程中随时间变化的压降特征分析。实验范围包括质量通量为43.8-3070 kg / m〜2 s,壁温为100℃-171.2℃。在所有情况下,测试段的进水口都被过冷至72.9至99.6℃。使用的入口压力为1.1-230.5 kPa(表压)。

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