Modélisation de l'évaporation de gouttes multi-composants

REFERENCES BIBLIOGRAPHIQUES[10] K. Gartung, ST. Arndt, CH. Seibel, Vaporization of Multicomponent Fuel Dropletsnumerical and Experimental Evaluation, 18 th Inst. On Liquid Atomization and SpraySystems, Zaragoza, Spain, September 9-11, 2002.[11] J. Strengele, K. Prommersberger, M. Willmann, S. Wittig, Experimental andTheoretical of One- and Two-component Droplet Vaporization in a High PressureEnvironment, Int. J. of Heat and Mass Transfer, Vol. 42, pp.2683-2694, 1999.[12] B. Abramzon, W.A. Sirignano, Approximate Theory of Single Droplet Vaporizationin a Convective Field : Effect of Variable Properties, Stefan Flow and TranscientLiquid Heating, vol. 1, Thermal Eng. Joint Conf., ASME JSME, pp. 11-18, 1987.[13] W.E. Ranz, W.R. Marshall, Evaporation from Drops, Chem. Eng. Progr., vol. 48,pp.141-146, 173-180, 1952.[14] J. Tamim, W.L.H. Hallett, A Continuous Thermodynamics Model forMulticomponent Droplet Vaporization, Chemical Engineering Science, vol. 50, N° 18,pp. 2933-2942, 1995.[15] W.L.H. Hallett, A simple model for the vaporization of droplets with large numbersof components, Combustion and Flame, vol. 121 pp. 334-344, 2000.[16] W.L.H. Hallett, C. Grimwood, A Simple Continuous Mixture Evaporation Modelwith Multiple Distribution Functions,http://www.genie.uottawa.ca/profs/hallett/hallettqs.pdf.[17] Z. Abdel-Qader, W.L.H. Hallett, The Role of Liquid Mixing in Evaporation ofComplex Multicomponent Mixtures : Modeling using Continuous Thermodynamics –II, http://by.genie.uottawa.ca/profs/hallett/hallettld.pdf.[18] K.G. Harstadt, P.C. Le Clercq, J. Bellan, Modeling Evaporation of Jet A, JP-7 andRP-1 drops at 1 to 15 bars, Combustion and Flame, Vol. 137 (1-2), pp. 163-177, 2004.[19] M. Burger, R. Schmehl, K. Prommersberger, O. Schäfer, R. Koch, S. Wittig,Droplet Evaporation Modeling by the Distillation Curve Model: Accounting forKerosene Fuel and Elevated Pressures, Int. Journal of Heat and Mass Transfer,Vol. 46, pp. 4403-4412, 2003.306