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Experimental Investigation and Numerical Simulation of Two-Phase Flow in a Large-Diameter Horizontal Flow Line Vertical Riser

机译:大直径水平流线立管中两相流的实验研究与数值模拟

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摘要

As oil and gas field development moves further into deep seas, maximizing hydrocarbon extraction at an acceptable cost is one of the greatest challenges facing the industry today. In this regard, considerable attention has been given to understanding the flow behavior in long and deep flow line risers of different topologies through transient multiphase simulation. However, the application of the large diameter to the above scenario is still an unresolved issue creating a great deal of uncertainty. This is mainly due to the limitation of the available experimental and field data being confined to much smaller diameters. In view of the aforementioned, an experimental campaign to investigate the flow behavior in a 254-mm nominal-diameter horizontal flow line vertical riser has been performed. A numerical model to study the dynamic behavior of the large-diameter horizontal flow line vertical riser system is also developed using OLGA software with the intention of identifying the capability of this software. This article presents the comparison of the simulation and experimental data in terms of near riser base and flow line pressure variations along with flow regime predictions. The existence of the multiple roots in the OLGA code is also reported for the first time. Additionally, a review on the state-of-the-art application of the code and analysis of the numerical experiment performance of the code are included.
机译:随着油气田的开发进一步向深海发展,以可接受的成本最大程度地开采碳氢化合物是当今行业面临的最大挑战之一。在这方面,已经给予了相当大的关注,以通过瞬态多相模拟来了解不同拓扑结构的长深流线立管中的流动行为。然而,将大直径应用于上述情况仍然是一个未解决的问题,从而带来了很大的不确定性。这主要是由于将可用的实验数据和现场数据限制在小得多的直径上。鉴于上述情况,已经进行了一项实验活动,以研究在254毫米标称直径水平流线垂直立管中的流动行为。为了确定该软件的功能,还使用OLGA软件开发了一个用于研究大直径水平流线垂直立管系统动力学行为的数值模型。本文根据近立管基部和流线压力变化以及流态预测对模拟和实验数据进行了比较。还首次报告了OLGA代码中多个根的存在。此外,还包括对代码的最新应用程序的回顾以及对代码的数字实验性能的分析。

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