Evaluation of Flow Characteristics in an Oil-Water Separator Using Computational Fluid Dynamics

T. Potter, Tathagata Acharya
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Abstract

Multiphase separators on production platforms are among the first equipment through which well fluids flow. Based on functionality, multiphase separators can either be two-phase that separate oil from water, or three-phase that separate oil, natural gas, and water. Separator performances are often evaluated using mean residence time (MRT) of the hydrocarbon phase. MRT is defined as the amount of time a given phase stays inside the separator. On field, operators usually measure MRT as the ratio of active volume occupied by each phase to the phase volumetric flowrate. However, this method may involve significant errors as the oil-water interface height is obtained using level controllers and the volume occupied by each phase is calculated assuming the interface can be extrapolated from the weir back to the separator inlet. In this study, authors perform computational fluid dynamics (CFD) on a two-phase horizontal separator to evaluate MRT as a function of varying water volume flowrates (water-cut) in a mixture of water and oil. The authors use residence time distributions (RTD) to obtain MRT at each water-cut — a method that results in significantly more accurate results than the regular method used by operators. The numerical model is developed with commercial software package ANSYS Fluent. The code uses the Eulerian multiphase model along with the k-ε turbulence model. The simulation results show agreement with experiments performed by previous researchers. Additional simulations are performed to assess the effect of various separator internals on separator performance. Simulation results suggest that the model developed in this study can be used to predict performances of two-phase liquid-liquid separators with reasonable accuracy and will be useful towards their design to improve performances under various inlet flow conditions.
油水分离器流动特性的计算流体力学评价
生产平台上的多相分离器是井中流体首先流过的设备之一。根据功能,多相分离器可以是分离油和水的两相分离器,也可以是分离油、天然气和水的三相分离器。分离器的性能通常用烃相的平均停留时间(MRT)来评价。MRT定义为给定相位停留在分离器内的时间。在现场,作业者通常将MRT测量为每相所占的有效体积与相体积流量之比。然而,这种方法可能会有很大的误差,因为油水界面高度是使用液位控制器获得的,并且每个相占用的体积是在假设界面可以从堰外推到分离器入口的情况下计算的。在这项研究中,作者对两相水平分离器进行了计算流体动力学(CFD),以评估MRT作为水与油混合物中不同体积流量(含水率)的函数。作者使用停留时间分布(RTD)来获得每个含水点的MRT,这种方法比运营商使用的常规方法得到的结果要准确得多。利用商业软件ANSYS Fluent建立了数值模型。该代码使用欧拉多相模型以及k-ε湍流模型。仿真结果与前人的实验结果一致。另外进行了模拟,以评估各种分离器内部对分离器性能的影响。仿真结果表明,所建立的模型可以较准确地预测两相液液分离器的性能,并有助于两相液液分离器在不同进口流动条件下的性能设计。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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