首页> 外文会议>Final IIR-Gustav Lorentzen Conference on Natural Working Fluids at Purdue >HEAT TRANSFER AND PRESSURE DROP CHARACTERISTICS OF EVAPORATING CARBON DIOXIDE IN MICROCHANNEL TUBES
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HEAT TRANSFER AND PRESSURE DROP CHARACTERISTICS OF EVAPORATING CARBON DIOXIDE IN MICROCHANNEL TUBES

机译:微通道管中蒸发二氧化碳的传热和压降特性

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This paper provides evaporation heat transfer and pressure drop data for carton dioxide (CO{sub}2. R-744) in a flat multiport extruded (MPE) aluminium tube. The tube had 25 circular ports/channels with 0.79 mm inner diameter. Data are presented for the following range of variables: Mass flux 200-600 kg/(m{sup}2s), evaporation temperature 0-20°C, and heat flux 5-20 kW/m{sup}2. The overall heat transfer coefficient was measured for water-to-CO{sub}2 heat transfer, and the CO{sub}2-side heat transfer coefficient was arrived at by using a modified Wilson plot technique to calibrate an equation for the water-side heat transfer coefficient The measured CO{sub}2 evaporation heat transfer coefficients lay in the range between 5,000 and 15,000 W/(m{sup}2K). From a certain vapour fraction upwards, the heat transfer coefficient dropped significantly. This effect was most pronounced for high mass fluxes and evaporation temperatures. As accompanying paper (Pettersen et al., 2000a) presents the results from supercritical-pressure heat transfer and pressure-drop experiments.
机译:本文提供了在挤出(MPE)铝管的扁平多端口纸箱二氧化碳(CO {子} 2。R-744)蒸发的热传递和压降数据。该管具有与0.79毫米内径25的圆形端口/信道。数据表示为以下范围的变量:质量流量200-600公斤/(米{SUP} 2S),蒸发温度0-20℃,热通量5-20千瓦/米{SUP} 2。总传热系数是通过使用改进的威尔逊情节技术来校准所述水的方程为水 - CO {子} 2的热传递,和CO {子} -2-侧传热系数乃测量在侧的传热系数所测得的CO {子} 2蒸发的传热系数躺在范围5000和15000 W之间/(米{SUP} 2K)。从某一蒸气馏分向上,热传递系数显著下降。这种效果是最明显的高质量通量和蒸发温度。作为伴随纸(Pettersen的等人,2000年)从呈现超临界压力的热传递和压降的实验结果。

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