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首页> 外文期刊>The Korean journal of chemical engineering >Modeling of low viscosity oil-water annular flow in horizontal and slightly inclined pipes: Experiments and CFD simulations
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Modeling of low viscosity oil-water annular flow in horizontal and slightly inclined pipes: Experiments and CFD simulations

机译:水平和微倾斜管道中低粘度油水环流的建模:实验和CFD模拟

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To characterize the effect of pipe inclination, low viscosity, flow rate and inlet water cut on annular flow pattern, a low viscosity oil-water two-phase annular flow in horizontal and slightly inclined (+1A degrees, +3A degrees and +5A degrees) pipes with diameter of 20 mm has been experimentally investigated. A modified VOF model based on the CFD software package FLUENT was used to predict the in-situ oil fraction and pressure drop. The experimental data indicate that annular flow appears at a medium-high water cut. The slip ratio increases with flow rate increase but decreases with increasing water cut. The changes are more significant as the degree of inclination increases. Pressure drop is strongly dependent on flow rate, as it increases rapidly as inlet flow rate increase. Good agreement between the experimental data and calculated results of slip ratio and pressure drop was obtained.
机译:为了表征管道倾角,低粘度,流量和切入水对环形流型的影响,水平和略微倾斜(+ 1A度,+ 3A度和+ 5A度)的低粘度油水两相环形流)直径为20毫米的管道已经过实验研究。使用基于CFD软件包FLUENT的改良的VOF模型来预测原位油分和压降。实验数据表明,环形水流出现在中高含水率处。滑移率随流量的增加而增加,但随含水率的增加而减小。随着倾斜度的增加,变化更加明显。压降主要取决于流量,因为它会随着入口流量的增加而迅速增加。实验数据与滑移率和压降的计算结果之间具有良好的一致性。

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