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FLOW-INDUCED VOID FRACTION TRANSITION PHENOMENON IN TWO-PHASE FLOW

机译:两相流中的流动引起的空隙率转变现象

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The flow-induced void fraction transition phenomenon was observed in an upward air-water two-phase flow in a vertical pipe with inner diameter D=200 mm and height z=25 m. As the two-phase flow develops in a vertical pipe, the void fraction increases firstly in the flow direction in bubbly flow, then decreases in the flow direction, finally increase again. The flow-induced void fraction transition shows an N-shaped changing manner. The present experimental investigation revealed that this phenomenon was attributed to the formation and the growth of local dominant large bubbles in the flow. According to the bubble sizes and behaviors observed in the experiment, the flow regimes were classified into bubbly, churn and slug flows in a vertical large-diameter pipe. The drift velocities in the three flow regimes were measured in this paper. New constitutive equation for drift velocities in bubbly, churn and slug flows was proposed and confirmed in this study. The flow-induced void fraction transition in N-shaped manner can be predicted by using the drift flux model with the newly developed constitutive equations.
机译:在内径D = 200 mm,高度z = 25 m的垂直管中,在向上的空气-水两相流中观察到了由流动引起的空隙分数转变现象。随着垂直管中两相流的发展,气泡率在气泡流中首先沿流向增大,然后沿流向减小,最后再次增大。流动引起的空隙率变化呈N形变化。目前的实验研究表明,这种现象归因于流动中局部主要大气泡的形成和增长。根据实验中观察到的气泡大小和行为,在垂直大直径管道中,将流态分为气泡,搅动和团状流。本文测量了三种流动状态下的漂移速度。提出并验证了气泡,搅动和团状流中漂移速度的新本构方程。通过使用具有新开发的本构方程的漂移通量模型,可以预测N形流动引起的空隙率转变。

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