Translational velocities of elongated bubbles in continuous slug flow

The translational velocities of elongated bubbles in continuous slug flow were measured for various flow rates, pipe inclinations and pipe diameters. Measurements were carried out by cross-correlating the output signals of consecutive optical fiber probes and by image processing technique. In addition, the velocities of single elongated bubbles in a stagnant and in a flowing liquid were measured by the same techniques. For all cases the measured velocities were compared to appropriate correlations. The measured velocities of single elongated bubbles were in all cases predicted quite well by the correlations while the velocities in continuous slug flow, for certain cases, were considerably underpredicted. This discrepancy is ascribed to the influence of the dispersed bubbles in the liquid slug region. A simplified model is proposed to calculate the translational velocity in continuous slug flow. The results of the model compare well with the measured translational velocities of elongated bubbles in continuous slug flow. 2002 Elsevier Science Ltd. All rights reserved.

[1]  M. E. Ryan,et al.  Velocities of extended bubbles in inclined tubes , 1986 .

[2]  Neima Brauner,et al.  Holdup of the liquid slug in two phase intermittent flow , 1985 .

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

[4]  Kjell H. Bendiksen,et al.  An experimental investigation of the motion of long bubbles in inclined tubes , 1984 .

[5]  Robert S. Brodkey,et al.  The phenomena of fluid motions , 1967 .

[6]  T. Benjamin Gravity currents and related phenomena , 1968, Journal of Fluid Mechanics.

[7]  D. Barnea Effect of bubble shape on pressure drop calculations in vertical slug flow , 1990 .

[8]  L. Shemer,et al.  The relation between the Taylor bubble motion and the velocity field ahead of it , 1999 .

[9]  Yehuda Taitel,et al.  Two-Phase Slug Flow , 1990 .

[10]  I. N. Alves,et al.  Drift velocity of elongated bubbles in inclined pipes , 1993 .

[11]  G. Wallis One Dimensional Two-Phase Flow , 1969 .

[12]  N. Draper,et al.  Applied Regression Analysis , 1967 .

[13]  A. Johnson,et al.  A PHYSICALLY BASED CORRELATION FOR THE EFFECTS OF POWER LAW RHEOLOGY AND INCLINATION ON SLUG BUBBLE RISE VELOCITY , 1995 .

[14]  Zai-Sha Mao,et al.  An experimental study of gas-liquid slug flow , 1989 .

[15]  D. Dumitrescu Strömung an einer Luftblase im senkrechten Rohr , 1943 .

[16]  T. Z. Harmathy,et al.  Velocity of large drops and bubbles in media of infinite or restricted extent , 1960 .

[17]  R. van Hout,et al.  SPATIAL DISTRIBUTION OF VOID FRACTION WITHIN A LIQUID SLUG AND SOME OTHER RELATED SLUG PARAMETERS , 1992 .

[18]  R. Bonnecaze,et al.  Holdup and pressure drop for two‐phase slug flow in inclined pipelines , 1971 .

[19]  A. Rashid Hasan,et al.  Predicting Multiphase Flow Behavior in a Deviated Well , 1988 .

[20]  R. van Hout,et al.  Evolution of statistical parameters of gas–liquid slug flow along vertical pipes , 2001 .

[21]  H. V. D. Akker,et al.  Measurements on wave propagation and bubble and slug velocities in cocurrent upward two-phase flow , 1997 .

[22]  A. Dukler,et al.  Hydrodynamic model for gas‐liquid slug flow in vertical tubes , 1983 .

[23]  Void fraction measurements in vertical slug flow: applications to slug characteristics and transition , 1989 .

[24]  J. Bendat,et al.  Measurement and Analysis of Random Data , 1968 .