Investigating the Mean Residence Time in a Two-Phase Oil-Water Separator Using Volume of Fluid Multiphase Theory in Computational Fluid Dynamics Simulation

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Abstract

Multiphase separators are essential to chemical units, especially in the oil and gas industry. Because separators are usually the first equipment installed in the oil and gas units, their performance directly affects other equipment. A two-phase oil-water separator was investigated in this study. Based on the average residence time reported for the pilot separator, the computational fluid dynamics (CFD) simulation was validated. The multiphase volume of fluid (VOF) theory in Ansys Fluent software is used for the simulation. Initially, the effect of halving the geometry from its line of symmetry was investigated to see if the halved geometry could replace the complete geometry in the simulation. After validation, the effect of four different inlet deflectors on the mean residence time (MRT) was investigated. A spherical inlet deflector and three plate inlet deflectors with varying angles were tested to examine the effects of inlet deflectors. Among the plate inlet deflectors, the one with an angle between the plates of 105 degrees had the highest MRT and the separator with an angle between the plates of 135 degrees had the lowest MRT. This is because of the fluid conduction by the separator and its collision with its wall. The spherical input deflector increases the MRT by 8.9% compared to the separator without the input deflector.
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应用计算流体力学模拟中流体多相体积理论研究两相油水分离器平均停留时间
多相分离器在化工设备中是必不可少的,特别是在石油和天然气工业中。由于分离器通常是安装在油气装置中的第一个设备,其性能直接影响到其他设备。研究了一种两相油水分离器。基于先导分离器的平均停留时间,对计算流体力学(CFD)模拟进行了验证。采用Ansys Fluent软件中的多相流体体积(VOF)理论进行仿真。最初,研究了将几何形状从对称线上减半的效果,看看减半的几何形状是否可以取代模拟中的完整几何形状。验证后,研究了四种不同的进口偏转板对平均停留时间的影响。通过对一个球形进口偏转板和三个不同角度的板式进口偏转板的试验,考察了进口偏转板的效果。其中,板间夹角为105°的板进口偏转板的MRT最高,板间夹角为135°的隔板的MRT最低。这是由于分离器的流体传导及其与壁面的碰撞。与没有输入偏转器的分离器相比,球形输入偏转器的MRT提高了8.9%。
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