Volumetric interfacial area prediction in upward bubbly two-phase flow
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[1] Mamoru Ishii,et al. Two-group interfacial area transport equations at bubbly-to-slug flow transition , 2000 .
[2] H. C. Ünal,et al. Maximum bubble diameter, maximum bubble-growth time and bubble-growth rate during the subcooled nucleate flow boiling of water up to 17.7 MN/m2 , 1976 .
[3] N. Zuber. ON THE DISPERSED TWO-PHASE FLOW IN THE LAMINAR FLOW REGIME. , 1964 .
[4] Christophe Morel. Modélisation multidimensionnelle des écoulements diphasiques gaz - liquide : application à la simulation des écoulements à bulles ascendants en conduite verticale , 1997 .
[5] R. Schiestel,et al. Modélisation et simulation des écoulements turbulents , 1993 .
[6] S. H. Park,et al. The Splitting of Drops and Bubbles by Turbulent Fluid Flow , 1973 .
[7] Nicholas P. Cheremisinoff,et al. Handbook of fluids in motion , 1983 .
[8] Said Elghobashi,et al. A two‐equation turbulence model for two‐phase flows , 1983 .
[9] F. Barre,et al. Overview of the numerical and computational developments performed in the frame of the CATHARE 2 code , 1995 .
[10] Mamoru Ishii. TWO-FLUID MODEL FOR TWO-PHASE FLOW , 1987 .
[11] Mamoru Ishii,et al. Interfacial area and nucleation site density in boiling systems , 1983 .
[12] Wei Yao,et al. Prediction of Parameters Distribution of Upward Boiling Two-Phase Flow With Two-Fluid Models , 2002 .
[13] M. Ishii,et al. Micro four-sensor probe measurement of interfacial area transport for bubbly flow in round pipes , 2001 .
[14] Mamoru Ishii,et al. One-group interfacial area transport of bubbly flows in vertical round tubes , 2000 .
[15] K. Nakao,et al. Coalescence and breakup of bubbles in liquids , 1977 .
[16] J. Marié,et al. Modélisation de la turbulence de la phase liquide dans un écoulement à bulles , 1984 .
[17] Won Kook Lee,et al. COALESCENCE BEHAVIOR OF TWO BUBBLES IN STAGNANT LIQUIDS , 1987 .
[18] Frédéric Risso,et al. THE MECHANISMS OF DEFORMATION AND BREAKUP OF DROPS AND BUBBLES , 2000 .
[19] Michel Lance,et al. PHASE DISTRIBUTION PHENOMENA AND WALL EFFECTS IN BUBBLY TWO-PHASE FLOWS , 1994 .
[20] Jean-Marc Delhaye. Some issues related to the modeling of interfacial areas in gas–liquid flows, II. Modeling the source terms for dispersed flows , 2001 .
[21] M. Ishii,et al. One-dimensional drift-flux model and constitutive equations for relative motion between phases in various two-phase flow regimes , 2003 .
[22] Claudie Grossetete. Caractérisation expérimentale et simulations de l'évolution d'un écoulement diphasique à bulles ascendant dans une conduite verticale , 1995 .
[23] Mamoru Ishii,et al. One-group interfacial area transport in vertical bubbly flow , 1998 .
[24] C. W. Stewart. Bubble interaction in low-viscosity liquids , 1996 .
[25] H. Blanch,et al. Bubble coalescence and break‐up in air‐sparged bubble columns , 1990 .
[26] T. R. Auton,et al. The lift force on a spherical body in a rotational flow , 1987, Journal of Fluid Mechanics.
[27] M. J. Lockett,et al. The influence of approach velocity on bubble coalescence , 1974 .
[28] Lawrence L. Tavlarides,et al. Description of interaction processes in agitated liquid-liquid dispersions , 1977 .
[29] Etienne Manon,et al. Contribution à l'analyse et à la modélisation locale des écoulements bouillants sous-saturés dans les conditions des réacteurs à eau sous pression , 2000 .
[30] Michael Z. Podowski,et al. MULTIDIMENSIONAL EFFECTS IN FORCED CONVECTION SUBCOOLED BOILING , 1990 .