Modeling Liquid Holdup in Pseudo-Slugs

Yilin Fan, E. Al-Safran, E. Pereyra, C. Sarica
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引用次数: 2

Abstract

Pseudo-slug flow is a sub-regime of intermittent flow that is characterized by short, undeveloped, frothy chaotic slugs, with translational velocity less than the mixture velocity of the fluids. Pseudo-slug flow does not comply with the basic characteristics of conventional unit-cell slug flow where liquid blocks the entire pipe cross-sectional area, and liquid is scooped at slug front, transferred to slug body, and shed back to liquid film. The liquid in pseudo-slug body is insufficient to reach the upper part of the pipe wall, resulting in only large wave with entrained gas bubbles at the bottom part of the pseudo slug body. Consequently, a significant reduction in the gas phase flowing area above the wave is formed, which increases the local gas velocity, entraining large volume of liquid droplets in the upper part of the slug body. Therefore, the pseudo-slug body can be divided into two regions, liquid film (wave) with entrained gas bubbles at the bottom, and gas core with entrained liquid droplets. The objective of this study is to develop a plausible physical model of the experimentally observed pseudo-slug liquid holdup phenomenon and model the physical and hydrodynamic behavior using a dimensional regression modeling approach. This paper discusses liquid and gas entrainment mechanisms within pseudo-slug body based on experimental observation. Previous experimental results show that the proposed dimensionless groups; namely, Stokes, Slippage, and Poiseuille are strongly correlated to pseudo-slug body liquid holdup experimental data and are capable of describing the experimentally observed physical behavior. A linearized regression model is developed to combine the liquid holdup proportionally in both regions of the pseudo-slug body (mentioned above) and correlate them to the experimentally measured total pseudo-slug liquid holdup using wire mesh sensor. A validation study of the proposed model with Fan (2017) experimental data shows good agreement, outperforming all other existing slug liquid holdup correlations.
伪段塞流是一种间歇流,其特征是短的、不发达的、泡沫状的混沌段塞流,其平动速度小于流体的混合速度。假段塞流不符合常规单胞段塞流的基本特征,即液体堵塞整个管道截面积,液体在段塞前部被舀出,转移到段塞体,再流回液膜。假段塞流体内的液体不足以到达管壁的上部,在假段塞流体底部只产生带有夹带气泡的大波。因此,形成了波上方气相流动面积的显著减小,使得局部气速增大,在段塞体上部夹带了大量的液滴。因此,伪段塞体可分为底部夹带气泡的液膜(波)和夹带液滴的气芯两个区域。本研究的目的是为实验观察到的伪段塞流含液现象建立一个合理的物理模型,并使用量纲回归建模方法对其物理和流体动力学行为进行建模。本文在实验观察的基础上,讨论了伪段塞体内部的液气夹带机理。先前的实验结果表明,所提出的无量纲群;即Stokes、Slippage和Poiseuille与伪弹塞体含液率实验数据有很强的相关性,能够描述实验观察到的物理行为。建立了一个线性回归模型,将上述两个区域的液含率按比例组合起来,并将其与实验测量的假段塞流总液含率相关联。利用Fan(2017)的实验数据对所提出的模型进行了验证研究,结果显示出良好的一致性,优于所有其他现有的段塞流含液率相关性。
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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