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首页> 外文期刊>International Journal of Heat and Mass Transfer >One-group interfacial area transport of bubbly flows in vertical round tubes
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One-group interfacial area transport of bubbly flows in vertical round tubes

机译:垂直圆管中气泡流的一组界面传输

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摘要

ln relation to the development of the interfacial area transport equation. the sink and source terms in an adiabatic bubbly t1ow system were modeled based on the mechanisms of bubble-bubble and bubble-turbulent eddy random collisions. respectively. The interfacial area transport mechanism was discussed based on the derived model. One-dimensional interfacial area transport equation with the derived sink and source terms was evaluated by using the area averaged flow parameters of adiabatic air water bubbly flows measured in 25.4 mm and 50.8 mm diameter tubes. The flow conditions of the data set covered most of the bubbly flow regime. including finely dispersed bubbly flow (inlet superficial gas velocity 0.04l4-3.90 m/s, superficial liquid velocity f 0.262-5.00 m/s, void fraction: l.27- 46.8/100). Excellent agreement was obtained between modeled and measured interfacial area concentrations within the average relative deviation of ll.6/100. It was recognized that the present model would be promising for the interfacial area transport of the examined bubbly flows.
机译:关于界面面积迁移方程的发展。绝热气泡系统中的汇和源项是基于气泡和涡流涡流随机碰撞的机理建模的。分别。基于导出的模型讨论了界面传输机制。通过使用在直径为25.4 mm和50.8 mm的管道中测量的绝热空气气泡流的面积平均流量参数,评估了具有导出的汇和源项的一维界面面积传输方程。数据集的流动条件涵盖了大多数气泡流状态。包括细分散的气泡流(入口表观气体速度0.04l4-3.90 m / s,表观液体速度f 0.262-5.00 m / s,空隙率:1.27-46.8 / 100)。在平均相对偏差ll.6 / 100之内,建模和测量的界面区域浓度之间获得了极好的一致性。公认的是,本模型对于所检查的气泡流的界面区域传输将是有希望的。

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