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Flow pattern of boiling in micro-channel by numerical simulation

机译:数值模拟的微通道沸腾流动规律

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Boiling flows of R-134a and R-22 fluids in a 0.50 mm circular channel have been simulated to analyze bubbly flow, bubbly/slug flow, slug flow and slug/semi-annular flow depending on bubble evolution. The vapor-liquid interface was captured using VOF method. We studied the behavior of bubble growth and coalescence related to flow pattern transitions (bubbly/slug flow to slug flow, slug flow to slug/semi-annular flow) and analyzed the effect of fluid properties on transition lines. Some parameters, including heat flux, mass velocity, ONB point, vapor velocity, bubble lifting diameter, growth rate and generation frequency, have been analyzed in detail. The results show that bubble growth and coalescence are important factors for flow pattern transitions. The flow patterns at the micro-channel outlet predicted by simulation were in agreement with phenomena observed in experiments for bubbly/slug flow, slug flow and slug/semi-annular flow. In addition, the peak bubble frequency at the outlet was predicted and the general shape of the bubble frequency distribution at the outlet from simulation was found to be consistent with the achieved experimental results.
机译:已经对R-134a和R-22流体在0.50 mm圆形通道中的沸腾流动进行了模拟,以分析气泡的流动,气泡/团状流,团状流和团状/半环形流。使用VOF方法捕获气液界面。我们研究了与流型转变(气泡/团状流到团状流,团状流到团状/半环流)相关的气泡生长和聚结行为,并分析了流体特性对过渡线的影响。详细分析了一些参数,包括热通量,质量速度,ONB点,蒸气速度,气泡上升直径,生长速率和产生频率。结果表明,气泡的增长和聚结是流型转变的重要因素。通过模拟预测的微通道出口处的流动模式与在实验中观察到的气泡/团状流,团状流和团状/半环形流的现象相一致。另外,预测了出口处的峰值气泡频率,并且通过仿真发现出口处的气泡频率分布的总体形状与所获得的实验结果一致。

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