Physics of Fluids
Search:
   
 
 
 
Previous Article
Thermal convection of a viscoplastic liquid with high Rayleigh and Bingham numbers
We consider the effect of yield stress on the Rayleigh–Bénard convection of a viscoplastic material. First we consider the model problem of convection in a differentially heated loop, whi...
Next Article
Effects of geometric shape on the hydrodynamics of a self-propelled flapping foil
The hydrodynamics of a free flapping foil is studied numerically. The foil undergoes a forced vertical oscillation and is free to move horizontally. The effect of chord-thickness ratio is investigated...

Lattice Boltzmann simulation of the rise and dissolution of two-dimensional immiscible droplets

Phys. Fluids 21, 103301 (2009); doi:10.1063/1.3253385

Published 22 October 2009

You are not logged in to this journal. Log in

Cheng Chen and Dongxiao Zhang
The Sonny Astani Department of Civil and Environmental Engineering, University of Southern California, Los Angeles, California 90089, USA
We used a coupled multiphase lattice Boltzmann (LB) model to simulate the dissolution of immiscible liquid droplets in another liquid during the rising process resulting from buoyancy. It was found that there existed a terminal rise velocity for each droplet, and there was a power law relationship between the Eötvös (Eo) number and the terminal Reynolds (Re) number. Our simulation results were in agreement with the empirical correlation derived for predicting bubble rise. When more than two identical droplets rose simultaneously in a close proximity, the average terminal rise velocity was lower than that of a single droplet with the same size because of the mutual resistant interactions. The droplet trajectories at the noncentral positions were not straight because of the nonzero net horizontal forces acting on the droplets. The Damkohler (Da) and Peclet (Pe) numbers were varied to investigate the coupling between droplet size, flow field, dissolution at the interface, and solute transport. For a given Pe, increasing Da led to a higher dissolution rate. For a given Da, increasing Pe led to a higher dissolution rate. For a large Da and a small Pe, the process near the interface was diffusion limited, and the advective flow relative to the droplet resulting from droplet rise was unable to move the accumulated solute away from the interface quickly. In this case, it was favorable to split the single droplet into as many small ones as possible in order to increase the interface area per unit mass and consequently enhance the whole dissolution process. For a small Da and a large Pe, the process was dissolution limited near the interface. The mass of accumulated solute near the interface was little, so the advective flow at the top side of the droplet was able to clean the solute quickly. In this case it was favorable to keep the droplet as a single one in order to obtain a high rise velocity and consequently enhance the whole dissolution process. By studying the coupling between Da and Pe, we qualitatively proposed to construct a Da-Pe phase plane and found the interface dividing the plane into regions 1 and 2. Region 1 was the collection of points where it was favorable to break down the droplet into as many small ones as possible in order to accelerate dissolution, while region 2 was the collection of points where it was favorable to keep the droplet in a single one for the same purpose. Based on our LB simulations, we found that the interface was an increasing function of Pe. Region 1 was the portion above the interface, while region 2 was the portion below it. In real applications, if both Pe and Da are obtained, it will be easy to judge whether it is favorable to break down the droplet or not in order to accelerate dissolution by checking whether (Pe, Da) falls in region 1 or 2. ©2009 American Institute of Physics
History: Received 20 June 2009; accepted 30 September 2009; published 22 October 2009
Permalink: http://link.aip.org/link/?PHFLE6/21/103301/1
BUY THIS ARTICLE   (US$24)
Download PDF (1037 kB) View Cart

KEYWORDS and PACS

Keywords
PACS

RELATED DATABASES


To view database links for this article,
you need to log in.
To view database links for this article,
you need to log in.

PUBLICATION DATA

ISSN:
1070-6631 (print)   1089-7666 (online)
Publisher:
AIP is a member of CrossRef AIP

REFERENCES (28)

For access to fully linked references, you need to log in. For access to fully linked references, you need to Log in.
  1. X. Xu, S. Chen, and D. Zhang, “Convective stability analysis of the long-term storage of carbon dioxide in deep saline aquifers,” Adv. Water Resour. 29, 397 (2006).
  2. S. Rapaka, S. Chen, R. Pawar, P. Stauffer, and D. Zhang, “Nonmodal growth of perturbations in density-driven convection in porous media,” J. Fluid Mech. 609, 285 (2008).
  3. D. W. Moore, “The rise of a gas bubble in a viscous liquid,” J. Fluid Mech. 6, 113 (1959).
  4. T. D. Taylor and A. Acrivos, “On the deformation and drag of a falling viscous drop at low Reynolds number,” J. Fluid Mech. 18, 466 (1964).
  5. J. G. Hnat and J. D. Buckmaster, “Spherical cap bubbles and skirt formation,” Phys. Fluids 19, 182 (1976).
  6. X. Frank, D. Funfschilling, N. Midoux, and H. Z. Li, “Bubbles in a viscous liquid: Lattice Boltzmann simulation and experimental validation,” J. Fluid Mech. 546, 113 (2005).
  7. S. E. Kentish, G. W. Stevens, and H. R. C. Pratt, “Measurement of drop rise velocities within a Kühni extraction column,” Ind. Eng. Chem. Res. 36, 4928 (1997).
  8. M. R. Snyder, O. M. Knio, J. Katz, and O. P. Le Maître, “Numerical study on the motion of microscopic oil droplets in high intensity isotropic turbulence,” Phys. Fluids 20, 073301 (2008).
  9. D. Rodrigue, “Generalized correlation for bubble motion,” AIChE J.47, 39 (2001).
  10. S. Chen and G. D. Doolen, “Lattice Boltzmann method for fluid flows,” Annu. Rev. Fluid Mech. 30, 329 (1998).
  11. D. Zhang, R. Zhang, S. Chen, and W. E. Soll, “Pore scale study of flow in porous media: Scale dependency, REV, and statistical REV,” Geophys. Res. Lett. 27, 1195, doi:10.1029/1999GL011101 (2000).
  12. C. Chen, A. I. Packman, and J. F. Gaillard, “Pore-scale analysis of permeability reduction resulting from colloid deposition,” Geophys. Res. Lett. 35, L07404, doi:10.1029/2007GL033077 (2008).
  13. X. Shan and H. Chen, “Lattice Boltzmann model for simulation flows with multiple phases and components,” Phys. Rev. E 47, 1815 (1993).
  14. X. Shan and H. Chen, “Simulation of nonideal gases and liquid-gas phase transitions by the lattice Boltzmann equation,” Phys. Rev. E 49, 2941 (1994).
  15. Q. Kang, D. Zhang, and S. Chen, “Displacement of a two-dimensional immiscible droplet in a channel,” Phys. Fluids 14, 3203 (2002).
  16. C. Pan, M. Hilpert, and C. T. Miller, “Lattice-Boltzmann simulation of two-phase flow in porous media,” Water Resour. Res. 40, W01501, doi:10.1029/2003WR002120 (2004).
  17. M. G. Schaap, M. L. Porter, B. S. B. Christensen, and D. Wildenschild, “Comparison of pressure-saturation characteristics derived from computed tomography and lattice Boltzmann simulations,” Water Resour. Res. 43, W12S06, doi:10.1029/2006WR005730 (2007).
  18. N. Takada, M. Misawa, A. Tomiyama, and S. Hosokawa, “Simulation of bubble motion under gravity by lattice Boltzmann method,” J. Nucl. Sci. Technol. 38, 330 (2001).
  19. Q. Kang, D. Zhang, S. Chen, and X. He, “Lattice Boltzmann simulations of chemical dissolution in porous media,” Phys. Rev. E 65, 036318 (2002).
  20. Q. Kang, D. Zhang, and S. Chen, “Simulation of dissolution and precipitation in porous media,” J. Geophys. Res. 108, 2505, doi:10.1029/2003JB002504 (2003).
  21. T. Sato, R. T. Jung, and S. Abe, “Direct simulation of droplet flow with mass transfer at interface,” J. Fluids Eng. 122, 510 (2000).
  22. S. Ponce Dawson, S. Chen, and G. D. Doolen, “Lattice Boltzmann computations for reaction-diffusion equations,” J. Chem. Phys. 98, 1514 (1993).
  23. C. Chen, B. L. T. Lau, J. Gaillard, and A. I. Packman, “Temporal evolution of pore geometry, fluid flow, and solute transport resulting from colloid deposition,” Water Resour. Res. 45, W06416, doi:10.1029/2008WR007252 (2009).
  24. H. Uchida. editor, JSME Data Book: The Thermophysical Properties of Fluids (JSME, Tokyo, 1982).
  25. I. Aya, Direct Ocean Disposal of Carbon Dioxide, edited by N. Handa and T. Ohsumi (TERRAPUB, Tokyo, 1995), pp. 233-238.
  26. F. Takemura and A. Yabe, “Rising speed and dissolution rate of a carbon dioxide bubble in slightly contaminated water,” J. Fluid Mech. 378, 319 (1999).
  27. K. Sankaranarayanan, X. Shany, I. G. Kevrekidis, and S. Sundaresan, “Analysis of drag and virtual mass forces in bubbly suspensions using an implicit formulation of the lattice Boltzmann method,” J. Fluid Mech. 452, 61 (2002).
  28. X. Zhang and M. Lv, “Persistence of anomalous dispersion in uniform porous media demonstrated by pore-scale simulations,” Water Resour. Res. 43, W07437, doi:10.1029/2006WR005557 (2007).

CITING ARTICLES

For access to citing articles, you need to log in.
For access to citing articles, you need to Log in.