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TWO-PHASE REFRIGERANT MIXTURE (R-407C) FLOW IN SMOOTH MESO-SCALE HEAT EXCHANGERS

机译:中尺度换热器中的两相制冷剂混合物(R-407C)流动

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摘要

The paper presents results from an experimental study on refrigerant mixture flow (R-407C) in which the heat transfer coefficient was measured across a range of heat and mass fluxes. Flow characteristics in smooth horizontal meso-channels were measured for two different conditions, 1) subcooled and 2) saturated boiling with diameters of 1.59, 2.78, and 3.97 mm and a length of 50.8 mm in refrigerant mixture (R-407C). Experiments were performed at heat fluxes of 2 and 11 kW/m~2 for the subcooled boiling and 15 and 29 kW/m~2 for the saturated boiling. The mass flux was varied from 0.45 to 1.55 kg/min and the refrigerant was subcooled to 8℃. The saturated boiling experiments were conducted for ΔT_(sat)= 0 to 27℃. The heat transfer coefficients were found to be dependent on channel size, heat flux, and mass flux variations. For smaller channel diameters, the heat transfer rate significantly increased as compared to larger channel diameters. The results showed an increase of 100% in heat transfer coefficient when compared to traditional and micro-channel boiling characteristics.
机译:本文介绍了对制冷剂混合物流量(R-407C)进行的实验研究的结果,其中在整个热通量和质量通量范围内测量了传热系数。在两种不同条件下,测量了光滑水平中观通道的流动特性:1)过冷和2)饱和沸腾,制冷剂混合物(R-407C)的直径为1.59、2.78和3.97 mm,长度为50.8 mm。对于过冷沸腾,在2和11 kW / m〜2的热通量下,对于饱和沸腾,在15和29 kW / m〜2的热通量上进行了实验。质量流量在0.45至1.55 kg / min之间变化,制冷剂过冷至8℃。在ΔT_(sat)= 0至27℃的条件下进行了饱和沸腾实验。发现传热系数取决于通道尺寸,热通量和质量通量变化。对于较小的通道直径,与较大的通道直径相比,传热速率显着提高。结果表明,与传统和微通道沸腾特性相比,传热系数提高了100%。

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