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Numerical Simulation of Two-Phase Slug Flow Liquid-Carryover in a Converging T-junction

机译:聚合T型交界处两相块流动液体携带的数值模拟

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In the offshore platform, T-junction has been extensively used as preliminary gas-liquid separator due to its compact design. Frequently, a sudden slug generation causes liquid carryover issues leading to excessive liquid in the gas feed for downstream equipment. Geometry features of T-junction and slug flow are believed to be the root cause of this problem. Based on the literature review, previous works mostly focused on improving two-phase separation in the standard T-junctions without taking into account the impact of inlet flow regime. Moreover, there is no published research on the separation performance of converging T-junction, which is a promising design. The objective of this research is to numerically evaluate the hypothesis that converging T-junction yields better phase separation under slug flow compared with regular and reduced T-junctions. Three-dimensional Computational Fluid Dynamics (CFD) software FLUENT 17.2 and specialized User Defined Functions was utilized to study the evolutionary process of air-water slug flow and its phase separation behavior in converging T-junctions over eight different geometry designs. The incompressible Volume of Fluid (VOF) method was used to capture the transient distribution of segregated gas-liquid interface. The validity of the present model was compared with the experimental data taken from the air-water two-phase flow in 3-inch diameter main pipe of T-junction. The validated model gave a strong foundation to proceed with converging T-junction simulation. The research found that the converging T-junction can increase by upto 20% of separation efficiency compared with regular and reduced T-junction at the same operating conditions. Moreover, the converging T-junction with the main and converging diameter ratio of 0.67 and 0.4, respectively, to be optimal in improving the phase separation over a wide spectrum of air and water superficial velocities.
机译:在海上平台中,由于其紧凑的设计,T-Anction已被广泛用作初步气液分离器。通常,突然的SLUI产生导致液体携带问题导致下游设备的气体进料中过量的液体。据信T型连接和块流的几何特征是这个问题的根本原因。基于文献综述,以前的作品主要集中在不考虑入口流动制度的影响下改善标准T界中的两相分离。此外,没有关于会聚T-Anction的分离性能的公布研究,这是一个有前途的设计。该研究的目的是在数值上评估与常规和降低的T型连接相比,收敛T-Chinaption在SLUG流下产生更好的相分离的假设。利用三维计算流体动力学(CFD)软件流畅的17.2和专业用户定义功能,以研究空气水块流的进化过程及其相位分离行为在八种不同的几何设计中收敛T型。使用不可压缩的流体(VOF)方法的体积捕获隔离气液界面的瞬态分布。将本模型的有效性与从3英寸直径的T型连接件中的水水两相流量取出的实验数据进行了比较。经过验证的模型提供了强大的基础,继续进行融合T结仿真。该研究发现,与相同的操作条件下的常规和降低的T接合相比,聚合T型结可以增加20%的分离效率。此外,在提高空气和水位速度范围内的相分离和水位速度上,分别为0.67和0.4的主和会聚直径比的会聚的T型接头分别是最佳的。

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