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Simulation of gas-liquid two phase flow in upriser pipe of gas-lift systems

机译:气举系统上升管中气液两相流的模拟

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Gas-lift pumps are devices for lifting liquid phase incorporating the gas phase to be injected in the bottom of liquid column. They are widely used in various industrial applications such as oil extracting in petroleum industries. Gas-liquid flow being the main part of the flow through these systems, flowing in vertical pipes of gas-lift pumps has different regimes namely bubbly, slug, churn and annular. Considering each numerical method to be appropriate for modeling a certain flow regime, a suitable numerical approach is crucial to correct simulation of gas-liquid flow in upriser pipe of gas-lift systems. In this paper, two main approaches namely the volume of fluid (VOF) and Eulerian model are used for modeling of the two phase flow in the upriser pipe of the airlift system. The numerical results are compared with the experimental investigations to validate the numerical models. The two phase flow regimes simulated by the numerical method were compared with the available flow regime map in the literatures. The results indicate that using the VOF is more appropriate for modeling of bubbly and slug flows while the Eulerian model fits better for only annular flow regime.
机译:气举泵是用于提升液相的装置,该液相结合了要注入液相塔底部的气相。它们被广泛用于各种工业应用中,例如石油工业中的石油提取。气液流是通过这些系统的主要部分,在气举泵的垂直管中流动具有不同的状态,即起泡,弹塞,搅动和环形。考虑到每种数值方法都适合于对某种流动状态进行建模,因此一种合适的数值方法对于校正气举系统中上升管中的气液流动模拟至关重要。本文采用两种主要方法,即流体体积(VOF)和欧拉模型,对空运系统上升管中的两相流进行建模。将数值结果与实验研究进行比较以验证数值模型。将数值方法模拟的两相流态与文献中可用的流态图进行了比较。结果表明,使用VOF更适合于气泡流和弹团流的建模,而欧拉模型仅适用于环形流态。

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