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Experimental Study of the Influence of the Inside Surface Characteristics on the Carbon Dioxide Flow Boiling Heat Transfer Cofficient in a Horizontal Tube

机译:内表面特性对水平管中二氧化碳流沸腾换热系数影响的实验研究

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摘要

The CO2 heat pump water heater "ECO CUTE", which was commercialized in 2001, has a significant potential for energy conservation and greenhouse abatement. Shipments in fiscal 2007 expanded to 413,000 units. In order to encourage the broader use of "ECO CUTE", there is a need to develop a more compact and higher efficiency heat pump unit. The key element of the apparatus is always the evaporator. CRIEPI and Sumitomo Light Metal, Ltd. have studied CO_2 flow boiling heat transfer coefficient experimentally. In the previous report, mean heat flux was understood as being equivalent to mass velocity in significantly affecting the mean evaporating heat transfer coefficient (99.999% purity, without oil) in a horizontal smooth tube (outer diameter 6 mm, thickness 0.4 mm). In this report, the heat transfer coefficient and pressure drop of a smooth tube and 3 kinds of grooved tubes are measured. The test conditions are : CO_2 mass velocity from about 160 to about 660 kg/(m~2s)(heat flux from about 10 to about 40 kW/m2), pressures of CO_2 3.5MPa, 4.0MPa and 4.5MPa (saturation temperatures of 0, 5 and 10℃, respectively), tube lengths of 3.0m and 4.0m, quality at the inlet of the test section of 0.17 and CO_2 super heat at the outlet of test section of 5 K. Consequently, it is understood that the heat transfer coefficient of grooved tubes is higher than that of the smooth tube and in the higher mass velocity region, the heat transfer coefficient does not go below 400kg/m~2s. The difference in the heat transfer coefficient caused by the groove features is not clear.
机译:二氧化碳热泵热水器“ ECO CUTE”于2001年商业化,在节能和减少温室气体方面具有巨大潜力。 2007财年的出货量扩大到413,000个。为了鼓励更广泛地使用“ ECO CUTE”,需要开发一种更紧凑,效率更高的热泵单元。设备的关键元素始终是蒸发器。 CRIEPI和住友轻金属有限公司已通过实验研究了CO_2流动沸腾传热系数。在以前的报告中,平均热通量被理解为等效于质量速度,从而显着影响水平光滑管(外径6 mm,厚度0.4 mm)中的平均蒸发传热系数(纯度为99.999%,无油)。在此报告中,测量了光滑管和3种带槽管的传热系数和压降。测试条件为:CO_2质量速度为约160至约660 kg /(m〜2s)(热通量为约10至约40 kW / m2),CO_2的压力为3.5MPa,4.0MPa和4.5MPa(饱和温度为分别为0、5和10℃),管长为3.0m和4.0m,测试段入口处的质量为0.17,测试段出口处的CO_2过热为5K。因此,可以理解,沟槽管的传热系数高于光滑管,在较高的质量速度范围内,传热系数不会低于400kg / m〜2s。由凹槽特征引起的传热系数的差异尚不清楚。

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  • 来源
    《住友軽金属技報》 |2010年第2010期|p.103-111|共9页
  • 作者单位

    Thermal Engineering, Energy Engineering Research Laboratory, Central Research Institute of Electric Power Industry;

    No. 3 Department, Research & Development Center;

    No. 3 Department, Research & Development Center;

    College of engineering, Nihon University;

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