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Prediction of holdup in liquid slugs

Wybrane pełne teksty z tego czasopisma
Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
Correlations and models from the literature for the prediction of void fraction in liquid slugs are reviewed. It is shown that a mechanism that can explain the slug aeration in vertical, horizontal and inclined tubes has not yet been established. A new model that attributes the aeration of the liquid slug to a recurrent bubble entrainment from the Taylor bubble (TB) tail is introtuced. The bubble fragmentation is related to the rate of turbulent kinetic energy in the shear layer, which is formed at the TB wake as the liquid film plunges into the slug front. The model has been tested against experimental data available from the literature and was found to predict the effects of liquid and gas flow rates and physical properties, as well as tube diameter and inclination on the void fraction.
Słowa kluczowe
Rocznik
Tom
Strony
75--90
Opis fizyczny
Bibliogr. 20 poz., rys.
Twórcy
autor
  • Department of Fluid Mechanics and Heat Transfer, Faculty of Engineering, Tel Aviv University, Tel Aviv, Israel
autor
  • Department of Fluid Mechanics and Heat Transfer, Faculty of Engineering, Tel Aviv University, Tel Aviv, Israel
Bibliografia
  • 1. Gregory G. A., Nicholson M. K., AzizK.: Correlation of liquid, volume fraction in the slug for horizontal gas-liquid slug flow,Int, J. Multiphase Flow 4(1978), 33-39.
  • 2. Ferschneider G.: Ecoulement dipasiques gas-liquid, a poches et a bouchons en conduites, Revue de 'Institut Francais du Petroie, 38, 2(1983), 153-1B2.
  • 3. Dukler A. E., Hubbard M. G.: A mod,el for gas-liquid, slug .flow in horizontal and near horizontal tubes,I nd. Eng. Chem. Fund 14(1975), 337-347.
  • 4. Andreussi P., Bendiksen K.: An investigation of void fraction in liquid slugs for horizontal and, inclined gas-liquid pipe flow, Int. J, Multiphase Flow 15(1989), 937-946
  • 5. Felizola H,, Shoham O.: A unified model for slug flow in upward inclined, pipes, ASME J. Energy Resources Technology 117(1995), 1-6.
  • 6. Nuland S., Malvik L M., Valle A., Hedne P.: Gas fractions in slugs in densegas two-phase flow from horizontal to 60 degrees of inclination, The ASME Fluids Engineering Division Summer 1997,
  • 7. Malnes D.: Slug flow in vertical, horizontal and inclined pipes,IFE Report KR-E-83/002, 1983.
  • 8. Malnes D.: OLGAS 90.0 compared to vertical flow erperiments,IFE/KR/F91/158, 1991
  • 9. Fernandes R, C., Semiat R., Dukler A. E,: Hydrod,ynami,c model for gas liquid slug flow in vertical tubes, .AIChE J 29(1983), 981-989.
  • 10. Barnea D., BraunerN.: Holdup of liquid slug in two-phase intermittent flow, Int. J. Multiphase FIow 11(1985), 1-12.
  • 11. Brauner N.: The prediction of dispersed flow boundaries ,in liquid-liquid, and, gas-liquid systems,Int. J. Multiphase Flow 27(2001), 885-910
  • 12. Barnea D,, Shemer L,; Void fraction measumerents tn vertical slug flov application to slug characteristics and, transition, Int. J. Multiphase Flow 15(1989), 495-504
  • 13. Nicklin D.J., Wilkes J.O., Davidson J.F.: Two phase flow in vertical tubes, Trans, Inst. Chem. Eng. 40(1962), 61-68.
  • 14. Rajaratnam N,: Turbulent Jets, Developments in Water Science 5, Elsevier, Amsterdam 197
  • 15. Brodkey R. S.: The phenomena of fluid motions, Addison-Wesley, Reading, MA, 1969.
  • 16. Nusselt W,: Surface condensation of water, Z. Yer. De. Ing. 60(1916), 541546; 60 (1916), 569-575.
  • 17. Brauner N.: Roll wave celerity and average film thicknessin turbulent wavy film flow, Chem. Eng. Sci. 42(1987),265-273.
  • 18. Dukler A.E., Moalem Maron D., Brauner N.: .4 physical model for the minimum stable slug length, Chem. Eng. Sci. 4(1985), 1387-1397.
  • 19. Cheng H., Hill J . H., Azzopardi B. J.: A study of the bubble-to-slug transition, in vertical gas-liquid in columns of different diameter, Int. J. Multiphase Flow, 24(1998), 431-452.
  • 20. Brauner N., Ullmann L: Modeling of phase inversion phenomena in phase pipe flow, Int. J. Multiphase Flow, 28(2002) 1177-1204
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BWM2-0008-0025
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