EXPERIMENTAL CHARACTERIZATION OF SLUG FLOW IN VERTICAL DUCTS WITH AND WITHOUT DISPERSED BUBBLES THROUGH IMAGE ANALYSIS
DOI:
https://doi.org/10.56238/levv17n57-085Keywords:
Slug Pattern, Two-Phase Flow, Taylor BubbleAbstract
Two-phase slug flow is widely observed in industrial applications, especially in oil and gas production and transportation systems. In this regime, the interaction between Taylor bubbles and smaller-scale dispersed bubbles significantly influences the local hydrodynamics, modifying the liquid film behavior, interface morphology, and wake structure. In this study, a detailed experimental characterization of air-water flow in a vertical duct was performed using high-speed filming. The experimental methodology included high-speed filming for qualitative analysis of the interfaces. The images revealed regions of non-uniform distribution of dispersed bubbles, as well as collision, deformation, and coalescence phenomena. The results showed that the presence of small-scale bubbles significantly alters the flow around the Taylor bubble, reducing the intensity of recirculations in the wake and modifying the velocity profile in the liquid film. The results presented contribute to the understanding of the hydrodynamics of the slug pattern and provide an experimental basis for the validation of multiphase numerical models.
Downloads
References
BROWN, R.A.S. The Mechanics of Large Gas Bubbles in Tubes - 1. Bubble Velocities in Stagnant Liquids, Chinese Journal of Chemical Engineering, v.43, pp. 217-223, 1965.
BUGG, J.D.; SAAD, G.A. The velocity Field around a Taylor Bubble rising in a stagnant viscous fluid: numerical and experimental results. International Journal of Multiphase Flow, v. 28, pp 791-803, 2002.
CAMPOS, J.B.L.M.; NOGUEIRA, S.; RIETHMULLER, M.L.; PINTO, A.M.F.R. Flow in the nose region and annular film around a Taylor bublle rising through vertical columns of stagnant and flowing Newtonian liquids. Chemical Engineering Science, v. 61, pp. 845-857, 2006.
CAMPOS, J.B.L.M.; MAYOR, T.S.; FERREIRA, V.; PINTO, A.M.F.R. Hydrodynamics of Gas-Liquid Slug Flow Along Vertical Pipes in Turbulent Regime – An Experimental Study. Chemical Engineering Science, v. 61, pp. 845-857, 2008.
DE JESUS, J.M.; AHMAD, W.R.; KAWAJI, M. Experimental Study of Flow Structure in Vertical Slug Flow. Advances in Multiphase Flow, pp. 105–118, 1995.
KAWAJI, M., DEJESUS, J.M., TUDOSE, G. Investigation of flow structures in vertical slug flow. Nuclear Engineering and Design, v. 175, pp. 37-48, 1997.
MOISSIS, R.; GRIFFITH, P. Entrance effects in a two-phase slug flow. Journal of Heat Transfer, v. 84, pp. 29–39, 1962.
NOGUEIRA, S.; RIETHMULLER, M.L.; CAMPOS, J.B.L.M.; PINTO, A.M.F.R. Flow patterns in the wake of a Taylor bubble rising through vertical columns of stagnant and flowing Newtonian liquids: An experimental study. Chemical Engineering Science, v. 61, pp. 7199-7212, 2006.
PINTO, A.M.F.R.; PINHEIRO, M.N.; NOGUEIRA, S.; FERREIRA, V.D.; CAMPOS, J.B.L.M. Experimental study on the transition in the velocity of individual Taylor bubbles in vertical upward co-current liquid flow. Chemical Engineering Research and Design. v. 83, pp. 1103–1130, 2000.
VAN Hout, R.; GULITSKY, A.; BARNEA, D.; SHEMER, L., 2002. Experimental investigation of the velocity field induced by a Taylor bubble rising in stagnant water. International Journal of Multiphase Flow, Vol. 29, pp.579–596.