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Void fraction characteristics of adiabatic one-component vertically upward two-phase flows in circular and non-circular small diameter tubes

机译:圆形和非圆形小直径管中绝热单组分垂直向上两相流动的空隙馏分特性

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Evaporating and condensing heat transfer and pressure loss characteristics strongly depend oninterfacial structure of gas-liquid two-phase flows. Cross-sectional average void fraction is importantparameter on the one-dimensional analysis. Recently, since channel diameter becomes smaller, theeffect of surface tension on the flow behaviors would become stronger. This study deals with voidfraction characteristics of adiabatic two-phase flows using FC-72 as the working fluid. Crosssectionalaverage void fraction was measured by capacitance sensor. Circular, square and triangulartubes with the hydraulic diameter of 2 mm were used. Vertically upward flow was selected to evaluatefor axially symmetric phase distribution. From the results, it was confirmed that for the square andtriangular tube, void fraction became lower than the circular tube because liquid was accumulatedin the corner by surface tension. Although the lower void fraction leads to larger slip velocity, thegas-liquid interface of liquid film became smoother.
机译:蒸发和冷凝热传递和压力损失特性强烈依赖于气液两相流的界面结构。横截面平均空隙分数很重要一维分析的参数。最近,由于信道直径变小,因此表面张力对流动行为的影响将变得更加强大。这项研究涉及空隙使用FC-72作为工作流体的绝热两相流的馏分特性。划分通过电容传感器测量平均空隙率。圆形,正方形和三角形使用液压直径为2mm的管。选择垂直向上流量来评估用于轴对称相位分布。从结果中,证实了广场和三角形管,空隙率比圆形管低,因为液体累积在拐角处通过表面张力。虽然较低的空隙率导致更大的滑动速度,但是液体膜的气液界面变得更加光滑。

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