Theoretical analysis of fluid particle collisions in turbulent flow

Chemical Engineering Science

Volumn 54, Issue 21, 1999, Pages 4749-4755

  Hagesaether, Lars ^a   Jakobsen, Hugo A ^a   Svendsen, Hallvard F ^a  

^a NORWEGIAN UNIVERSITY OF SCIENCE AND TECHNOLOGY   (Norway)

Author keywords

Coalescence; Collision; Droplet oscillation; Film drainage; Forces; Simulation

Indexed keywords

BUBBLE COLUMNS; BUBBLE FORMATION; CHEMICAL REACTORS; COALESCENCE; COMPUTER SIMULATION; DROP FORMATION; PARTICLES (PARTICULATE MATTER); TURBULENT FLOW; VOLUME FRACTION;

COLLISION; DROPLET OSCILLATION; FILM DRAINAGE;

COMPUTATIONAL FLUID DYNAMICS;

COLLISION; DROPLET; MATHEMATICAL MODELING; TURBULENT FLOW;

EID: 0033231880     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0009-2509(99)00191-8     Document Type: Article

References (21)

1. Chesters, A. K. (1991). The modelling of coalescence processes in fluid-fluid dispersions: A review of current understanding. Transactions of the Institution of Chemical Engineers, 69, 259-270.
2. Clift, R., Grace, J. R., & Weber, M. E. (1978). In Bubbles, Drops, and Particles (p. 112). San Diego, USA: Academic Press.
3. Colin, C., Kamp, A. M., & Chesters, A. K. (1998). Measurement and prediction of bubble coalescence in turbulent pipe flows. Third International Conference on Multiphase Flows, ICMF98.
4. Cook, T. L., & Harlow, F. W. (1986). Vortices in bubble two phase flow. International Journal of Multiphase Flow, 12, 35-61.
5. Hagesaether, L., Luo, H., & Svendsen, H. F. (1996). The Modelling of Coalescence of Oscillating Liquid Drops, CHISA'96, Ref. No. 0383.
6. Hartland, S. (1969). The effect of circulation patterns on the drainage of the film between a liquid drop and a deformable liquid-liquid interface. Chemical Engineering Science, 24, 611-613.
7. Hartland, S., & Robinson, J. D. (1977). A model for an axisymmetric dimpled draining film. Journal of Colloid and Interface Science, 60, 72-81.
8. Ivanov, I. B. (1998). In: Thin Liquid Films Fundamentals and Applications (p. 391). New York, USA: Marcel Dekker.
9. Jeelani, S. A. K., & Hartland, S. (1991a). Collision of oscillating liquid drops. Chemical Engineering Science, 46, 1807-1814.
10. Jeelani, S. A. K., & Hartland, S. (1991b). Effect of approach velocity on binary and interfacial coalescence. Transactions of the Institution of Chemical Engineers, 69, 271-281.
11. Kirkpatrick, R. D., & Lockett, M. J. (1974). The influence of approach velocity on bubble coalescence. Chemical Engineering Science, 29, 2363-2373.
12. Klaseboer, E., Chevaillier, J. Ph., Masbernat, O., Gourdon, C. (1998). Drainage of the liquid film between drops colliding at constant approach velocity. Third International Conference on Multiphase Flows, ICMF98.
13. Lee, J. C., & Hodgson, T. D. (1968). Film flow and coalescence - I. Basic relations, film shape and criteria for interface mobility. Chemical Engineering Science, 23, 1375-1397.
14. Luo, H., & Svendsen, H. F. (1996). Modeling and simulation of binary approach by energy conservation analysis. Chemical Engineering Communication, 145, 145-153.
15. Middleman, S. (1998). In: An Introduction to Fluid Dynamics (p. 339). New York, USA: Wiley.
16. Montes, F. J., Galan, M. A., & Cerro, R. L. (1998). Mass transfer from oscillating bubbles in bioreactors, ISCRE 15, Reference 17-A.
17. Moørk, P. C. (1991). In: Overflate og Kolliodkjemi (p. 47). Trondheim, Norway: Institutt for industriell kjemi NTH.
18. Princen, H. M. (1963). Shape of a fluid drop at a liquid-liquid interface. Journal of Colloid Science, 18, 178-195.
19. Scheele, G. F., & Leng, D. E. (1971). An experimental study of factors which promote coalescence of two colliding drops in suspended water - I. Chemical Engineering Science, 26, 1867-1879.
20. Svendsen, H. F., & Luo, H. (1996). Modeling of approach processes for equal or unequal sized fluid particles. The Canadian Journal of Chemical Engineering, 74, 1-10.
21. Tsao, H. -T., & Koch, D. L. (1997). Observations of high reynolds number bubbles interacting with a rigid wall. Physics of Fluids, 9, 44.