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Two-phase flow transient simulation of severe slugging in pipeline-risers systems

机译:管道立管系统中严重粘滞的两相流动瞬态模拟

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Pipeline-risers systems are frequently encountered in the petroleum industry, especially in the offshore platforms. Single-phase flow does not involve significant troubles in the operations through these arrangements. However, during multiphase flow, flooding of the separation facilities could be expected due to the generation of severe slugs at the bottom of the riser. The size and frequency of the slugs are functions of the accumulation and displacement of liquid at the base of the riser and can be controlled with an adequate model. An improved transient model is presented to simulate severe slugging phenomenon in pipeline-risers systems. Gas penetration is described thoroughly since the first bubble penetrates into the riser until it reaches the top of it. The model presents improvements in the characteristics method applications including a correction for the gas density deviation caused by the nonfixed space-time resolution during the gas penetration. The results were compared with experimental data and previous models showing better accuracy. The model can be used to design new pipeline riser-systems or to adjust the operation of existing systems to prevent the occurrence of severe slug flow.
机译:石油工业经常遇到管道 - 立管系统,特别是在海上平台中。单相流不涉及通过这些布置在操作中的重大故障。然而,在多相流动期间,由于提升管底部的严重粘液产生,可以预期分离设施的洪水。块的尺寸和频率是液体在提升板的底部积聚和位移的功能,并且可以用足够的模型来控制。提出了一种改进的瞬态模型以模拟管道 - 立管系统中的严重粘性现象。由于第一个气泡渗透到提升板中,因此彻底地描述了气体渗透,直到它到达它的顶部。该模型呈现了特征方法应用的改进,包括在气体渗透期间不混凝的时空分辨率引起的气体密度偏差的校正。将结果与实验数据进行比较,以前的模型显示出更好的准确性。该模型可用于设计新的管道提升系统或调整现有系统的操作,以防止发生严重的块流。

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