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

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.

[1]  Y. Sato,et al.  Liquid velocity distribution in two-phase bubble flow , 1975 .

[2]  D. Kouremenos,et al.  Performance of a small air-lift pump , 1985 .

[3]  S. Patankar Numerical Heat Transfer and Fluid Flow , 2018, Lecture Notes in Mechanical Engineering.

[4]  E. T. White,et al.  The velocity of rise of single cylindrical air bubbles through liquids contained in vertical tubes , 1962 .

[5]  Pedram Hanafizadeh,et al.  Visual technique for detection of gas-liquid two-phase flow regime in the airlift pump , 2011 .

[6]  J. Brackbill,et al.  A continuum method for modeling surface tension , 1992 .

[7]  S. Van Geest Comparison of different air injection methods to improve gas-lift performance , 2000 .

[8]  Arnold Hartley Gibson,et al.  Hydraulics and its Applications , 1908, Nature.

[9]  Yusuf Chisti,et al.  Assure bioreactor sterility , 1992 .

[10]  Hiroharu Kato,et al.  A STUDY OF AN AIR-LIFT PUMP FOR SOLID PARTICLES , 1975 .

[11]  Pedram Hanafizadeh,et al.  Numerical simulation of two-phase flow in airlift pumps using the Physical Influence Scheme , 2010 .

[12]  E. Zukoski Influence of viscosity, surface tension, and inclination angle on motion of long bubbles in closed tubes , 1966, Journal of Fluid Mechanics.

[13]  Chia-Jung Hsu Numerical Heat Transfer and Fluid Flow , 1981 .

[14]  Pedram Hanafizadeh,et al.  REVIEW STUDY ON AIRLIFT PUMPING SYSTEMS , 2012 .

[15]  Wael H. Ahmed,et al.  Air-lift pumps characteristics under two-phase flow conditions , 2009 .

[16]  Amir Karimi,et al.  Effect of Step Geometry on the Performance of the Airlift Pump , 2011 .

[17]  F. de Cachard,et al.  A slugh-churn flow model for small-diameter airlift pumps , 1996 .

[18]  B. Launder,et al.  Mathematical Models of turbulence , 1972 .

[19]  A. E. Dukler,et al.  Modelling flow pattern transitions for steady upward gas‐liquid flow in vertical tubes , 1980 .

[20]  G. Trystram,et al.  Modeling and simulation of a large scale air lift fermenter , 1993 .

[21]  R. V. A. Oliemans,et al.  Influence of bubble size on the transition from low-Re bubbly flow to slug flow in a vertical pipe , 2002 .

[22]  F. de Cachard,et al.  Stability of small diameter airlift pumps , 1998 .

[23]  Pedram Hanafizadeh,et al.  Drag coefficient and strouhal number analysis of cylindrical tube in two phase flow , 2013 .

[24]  G. Csanady Turbulent Diffusion of Heavy Particles in the Atmosphere , 1963 .

[25]  F. A. Zenz Explore the potential of air-lift pumps and multiphase , 1993 .