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Experimental investigation of flow boiling in single minichannels with low mass velocities

机译:低速度下单个小通道内流沸腾的实验研究

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Flow boiling characteristics in a single minichannel with the aspect ratio of 2 (1.8 mm width and 0.9 mm height) are studied experimentally. Experiments are conducted for different values of the wall heat flux (in the range of 204.7-431.3 kW/m(2)) and low mass fluxes (G = 20, 40 and 60 kg M-2 S-1) at a constant inlet temperature of deionized water (approximately 70 degrees C). Effects of the heat and mass fluxes on the local two phase heat transfer coefficient and the total pressure drop are examined. A considerable attention is also paid to performing high speed flow visualization study to have qualitative information about the flow physics. The heat transfer coefficient shows an irregular trend with increasing heat flux or the vapor quality, while it increases with increasing mass flux. On the other hand, the pressure drop increases with an increase in the heat flux or in the exit vapor quality. For the lowest mass flux value considered, temperature jump or the critical heat flux (CHF) condition is shown to occur at higher heating powers.
机译:实验研究了纵横比为2(1.8毫米宽和0.9毫米高)的单个小通道中的沸腾特性。在恒定入口处针对壁热通量的不同值(范围为204.7-431.3 kW / m(2))和低质量通量(G = 20、40和60 kg M-2 S-1)进行实验去离子水的温度(约70摄氏度)。研究了热通量和质量通量对局部两相传热系数和总压降的影响。还非常重视执行高速流可视化研究,以获取有关流物理学的定性信息。传热系数随着热通量或蒸汽质量的增加而显示出不规则的趋势,而随着质量通量的增加而增加。另一方面,压降随着热通量或出口蒸气质量的增加而增加。对于所考虑的最低质量通量值,在较高的加热功率下会出现温度跃变或临界热通量(CHF)条件。

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