Interfacial area density in bubbly flow

Chemical Engineering and Processing: Process Intensification

Volumn 38, Issue 4-6, 1999, Pages 307-319

  Millies, Marco ^a   Mewes, Dieter ^a  

^a LEIBNIZ UNIVERSITY HANNOVER   (Germany)

Author keywords

Area density; Bubbly flow; Interfacial

Indexed keywords

BUBBLE COLUMNS; CHEMICAL REACTORS; COALESCENCE; ENERGY TRANSFER; INTEGRODIFFERENTIAL EQUATIONS; MASS TRANSFER; NUMERICAL ANALYSIS; PARTIAL DIFFERENTIAL EQUATIONS; PHASE INTERFACES; PIPE FLOW;

BUBBLY FLOW; MOMENTUM TRANSFER;

TWO PHASE FLOW;

BUBBLY FLOW; INTERFACE;

EID: 0033379641     PISSN: 02552701     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0255-2701(99)00022-7     Document Type: Article

References (36)

1. Akita K., Yoshida F. Bubble size, interfacial area and liquid-phase mass transfer coefficient in bubble columns. Ind. Eng. Chem. Proc. Des. Develop. 13(1):1974;84-91.
2. Nagel O., Kürten H., Hegner B. Die Stoffaustauschfläche in Gas/Flüssigkeits-Kontaktapparaten, Auswahlkriterien und Unterlagen zur Vergrößerung. Chem. Ing. Tech. 14:1973;913-920.
3. A.N. Kolmogoroff, J. Fluid Mech. 13, Part I (1962).
4. Mersmann A. Chem. Ing. Tech. 49(9):1977;679-691.
5. Blaß E. Bildung und Koaleszenz von Blasen und Tropfen. Chem. Ing. Tech. 60(12):1988;935-947.
6. Lin T.J., Tsuchiya K., Fau L.-S. Bubble flow characteristics in bubble columns at elevated pressure and temperature. AIChE J. 44(3):1998;545-560.
7. Guido-Lavalle G., Carrica P., Clausse A., Qazi M.K. A bubble number density constitutive equation. Nuc. Eng. Design. 152:1994;213-224.
8. C. Fleischer, M. Bierdel, G. Eigenberger, Prediction of bubble size distributions in G/L-contactors with population balances, in: Poster on the Third German/Japanese Symposium on Bubble Columns, Schwerte, 1994.
9. Valentas K.J., Amundson N.R. Breakage and coalescence in dispersed phase systems. I&EC Fundam. 5(4):1966;533-542.
10. S. Kalkach-Navarro, Two-fluid modeling of the bubbly/slug flow regime transition, Ph.D. thesis, Rensselear Polytechnic Institute, Troy, 1993.
11. J. Kelly, A four-field approach towards developing a mechanistic model for multiphase flow, Pacific Northwest Laboratory report PNL-SA-18878, DE93006572, 1993.
12. J. Grienberger, Untersuchung und Modellierung von Blasensäulen, Ph.D. thesis University Erlangen, Nürnberg, 1992.
13. R.P. Hesketh, Bubble breakage in turbulent liquid flow, Ph.D. thesis, University of Delaware, 1987.
14. C.H. Lee, A study of the hydrodynamics and bubble phenomena in gas-liquid airlift systems, Ph.D. thesis, Kansas State University, 1987.
15. Prince M.J., Blanch H.W. Bubble coalescence and break-up in air-sparged bubble columns. AIChE J. 36(10):1990;1485-1499.
16. Prince M.J., Blanch H.W. Transition electrolyte concentrations for bubble coalescence. AIChE J. 36(9):1990;1425-1429.
17. P.M. Wilkinson, Physical aspects and scale-up of high pressure bubble columns, Ph.D. thesis University Groningen, 1991.
18. Das R.K., Pattanayak S. Bubble to slug flow transition in vertical upward two-phase flow through narrow tubes. Chem. Eng. Sci. 49(13):1994;2163-2172.
19. Doubliez L. The drainage and rupture of a non-foaming liquid film formed upon bubble impact with a free surface. Int. J. Mult. Flow. 17(6):1991;783-803.
20. Brauer H. Grundlagen der Einphasen- und Mehrphasenströmungen. 1971;Sauerländer, Frankfurt am Main.
21. Marucci G., Nicodemo L. Coalescence of gas bubbles in aqueous solutions of inorganic electrolytes. Chem. Eng. Sci. 22:1967;1257-1265.
22. M. Millies, Phasengrenzflächen in Blasenströmungen, Chem.-Ing.-Tech. 68 (1996); 6, 660-669; 7, 790-795; 8, 927-933.
23. M. Millies, Phasengrenzflächen in Blasenströmungen, Chem.-Ing.-Tech. 68 (1996); 6, 660-669; 7, 790-795; 8, 927-933.
24. M. Millies, Phasengrenzflächen in Blasenströmungen, Chem.-Ing.-Tech. 68 (1996); 6, 660-669; 7, 790-795; 8, 927-933.
25. M. Millies, Phasengrenzflächen in Blasenströmungen, Chem.-Ing.-Tech. 68 (1996); 6, 660-669; 7, 790-795; 8, 927-933.
26. H.J. Schrag, Blasengrößen-Häufigkeitsverteilungen bei der Begasung von Gemischen organisch-chemischer Flüssigkeiten mit Stickstoff in Blasensäulen-Reaktoren, Dissertation RWTH Aachen, 1976.
27. G. Grund, Hydrodynamische Parameter und Stoffaustauscheigenschaften in Blasensäulen mit organischen Medien, Ph.D. thesis University of Oldenburg, 1988.
28. Sriram K., Mann R. Dynamic gas disengagement: a new technique for assessing the behavior of bubble columns. Chem. Eng. Sci. 32:1977;571-580.
29. Todtenhaupt E. Blasengrößenverteilung in technischen Begasungs-apparaten. Chem. Ing. Tech. 43(6):1971;336-342.
30. Griffith P., Wallis G.B. Two phase slug flow. J. Heat Transfer. 83:1961;307-320.
31. H. Duns, N.C.J. Ros, Vertical flow of gas and liquid mixtures from borcholes, in: Proceedings of the Sixth World Petroleum Congress, Part II, Frankfurt am Main, June 1963, pp. 419-450.
32. Molerus O., Kurtin M. Hydrodynamics of bubble columns in the liquid circulation regime. Chem. Eng. Sci. 41:1986;2685-2692.
33. Schumpe A., Grund G. The gas disengagement technique for studying gas holdup structure in bubble columns. Can. J. Chem. Eng. 64:1986;891-896.
34. Daly J.G., Patel S.A., Bukur D.B. Measurement of gas holdups and Sauter mean bubble diameters in bubble column reactors by dynamic gas disengagement method. Chem. Eng. Sci. 47(13/14):1992;3647-3654.
35. K.D. Kaufmann, Vergleich verschiedener Methoden der Phasengrenz-flächenmessung in Blasensäulen unter Einbeziehung höherer Drücke, IDEA Wissenschaftlich-technische Editionen, 1981.
36. T. Reith, Physical aspects of bubble dispersions in liquids, Dissertation TH Delft, 1968.