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Effect of buoyancy on the motion of long bubbles in horizontal tubes

Omer Atasi1,2,*, Sepideh Khodaparast2,†, Benoit Scheid1,‡, and Howard A. Stone2,§

  • 1Transfers, Interfaces and Processes, Universite Libre de Bruxelles, Brussels 1050, Belgium
  • 2Department of Mechanical and Aerospace Engineering, Princeton University, Princeton, New Jersey 08544, USA

  • *oatasi@ulb.ac.be
  • sepidehk@princeton.edu
  • bscheid@ulb.ac.be
  • §hastone@princeton.edu

Phys. Rev. Fluids 2, 094304 – Published 26 September, 2017

DOI: https://doi.org/10.1103/PhysRevFluids.2.094304

Abstract

As a confined long bubble translates along a horizontal liquid-filled tube, a thin film of liquid is formed on the tube wall. For negligible inertial and buoyancy effects, respectively, small Reynolds (Re) and Bond (Bo) numbers, the thickness of the liquid film depends only on the flow capillary number (Ca). However, buoyancy effects are no longer negligible as the diameter of the tube reaches millimeter length scales, which corresponds to finite values of Bo. We perform experiments and theoretical analysis for a long bubble in a horizontal tube to investigate the effect of Bond number (0.05<Bo<0.5) on the thickness of the liquid film and the bubble orientation at different capillary numbers 103<Ca<101. We investigate several features of the lubricating film around the bubble. (i) Due to the gravitational effects, the film deposited on the upper wall of the channel is thinner than the film at the bottom wall. We extend the available theory for the film thickness at the front of the bubble in a two-dimensional geometry at low capillary numbers Ca<103 and finite Bo to account for the effect of larger Ca. The resulting model shows very good agreement with the present experimental measurements. (ii) Due to the asymmetry in the liquid film thickness and the consequent drainage of the liquid from the top to the bottom of the tube, the bubble is inclined relative to the channel centerline and our side-view visualizations allow direct quantification of the inclination angle, which increases with both Bo and Ca. While the inclination angle at the top is smaller than that at the bottom of the tube, the average of these two values follows the predictions of a mass balance analysis in the central region of the bubble. (iii) The inclination of the bubble causes the thickness of the thin film at the back of the bubble to depend on the length of the bubble, whereas the thickness at the front of the bubble does not depend on the bubble length.

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References (20)

  1. F. P. Bretherton, The motion of long bubbles in tubes, J. Fluid Mech. 10, 166 (1961).
  2. F. Fairbrother and A. E. Stubbs, Studies in electro-endosmosis. Part VI. The “bubble-tube” method of measurement, J. Chem. Soc. 527 (1935).
  3. G. I. Taylor, Deposition of a viscous fluid on the wall of a tube, J. Fluid Mech. 10, 161 (1961).
  4. P. Aussillous and D. Quéré, Quick deposition of a fluid on the wall of a tube, Phys. Fluids 12, 2367 (2000).
  5. V. Suresh and J. B. Grotberg, The effect of gravity on liquid plug propagation in a two-dimensional channel, Phys. Fluids 17, 031507 (2005).
  6. Y. Zheng, H. Fujioka, and J. B. Grotberg, Effects of gravity, inertia, and surfactant on steady plug propagation in a two-dimensional channel, Phys. Fluids 19, 082107 (2007).
  7. A. de Lózar, A. Juel, and A. L. Hazel, The steady propagation of an air finger into a rectangular tube, J. Fluid Mech. 614, 173 (2008).
  8. Y. Han and N. Shikazono, Measurement of the liquid film thickness in micro tube slug flow, Int. J. Heat Fluid Flow 30, 842 (2009).
  9. R. Gupta, H. Hagnefelt, D. F. Fletcher, and B. S. Haynes, Proceedings of the Seventh International Conference on Multiphase Flow, Tampa, University of Florida, Gainesville, FL, 2010.
  10. S. Y. Leung, R. Gupta, D. F. Fletcher, and B. S. Haynes, Gravitational effect on Taylor flow in horizontal microchannels, Chem. Eng. Sci. 69, 553 (2012).
  11. M. H. Jensen, A. Libchaber, P. Pelcé, and G. Zocchi, Effect of gravity on the Saffman-Taylor meniscus: Theory and experiment, Phys. Rev. A 35, 2221 (1987).
  12. E. Brener, M. Rabaud, and H. Thomé, Effect of gravity on stable Saffman-Taylor fingers, Phys. Rev. E 48, 1066 (1993).
  13. R. Budwig, Refractive index matching methods for liquid flow investigations, Exp. Fluids 17, 350 (1994).
  14. S. Khodaparast, N. Borhani, and J. R. Thome, Application of micro particle shadow velocimetry μPSV to two-phase flows in microchannels, Int. J. Multiphase Flow 62, 123 (2014).
  15. N. Borhani, B. Agostini, and J. R. Thome, A novel time strip flow visualisation technique for investigation of intermittent dewetting and dryout in elongated bubble flow in a microchannel evaporator, Int. J. Multiphase Flow 53, 4809 (2010).
  16. M. D. Giavedoni and F. A. Saita, The rear meniscus of a long bubble steadily displacing a Newtonian liquid in a capillary tube, Phys. Fluids 11, 786 (1999).
  17. E. Klaseboer, R. Gupta, and R. Manica, An extended Bretherton model for long Taylor bubbles at moderate capillary numbers, Phys. Fluids 26, 032107 (2014).
  18. A. Sharma and E. Ruckenstein, Dewetting of solids by the formation of holes in macroscopic liquid films, J. Colloid Interface Sci. 133, 358 (1989).
  19. G. Callegari, A. Calvo, and J. P. Hulin, Dewetting processes in a cylindrical geometry, Eur. Phys. J. E 16, 283 (2005).
  20. A. Huerre, O. Theodoly, A. M. Leshansky, M.-P. Valignat, I. Cantat, and M.-C. Jullien, Droplets in Microchannels: Dynamical Properties of the Lubrication Film, Phys. Rev. Lett. 115, 064501 (2015).

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