A simplified model for bi-component droplet heating and evaporation

A simplified model for bi-component droplet heating and evaporation is developed and applied for the analysis of the observed average droplet temperatures in a monodisperse spray. The model takes into account all key processes, which take place during this heating and evaporation, including the distribution of temperature and diffusion of liquid species inside the droplet and the effects of the non-unity activity coefficient (ideal and non-ideal models). The effects of recirculation in the moving droplets on heat and mass diffusion within them are taken into account using the effective thermal conductivity and the effective diffusivity models. The previously obtained analytical solution of the transient heat conduction equation inside droplets is incorporated in the numerical code alongside the original analytical solution of the species diffusion equation inside droplets. The predicted time evolution of the average temperatures is shown to be reasonably close to the measured one, especially in the case of pure acetone and acetone-rich mixture droplets. It is shown that the temperatures predicted by the simplified model and the earlier reported vortex model are reasonably close. Also, the temperatures predicted by the ideal and non-ideal models differ by not more than several degrees. This can justify the application of the simplified model with the activity coefficient equal to 1 for the interpretation of the time evolution of temperatures measured with errors more than several degrees.

[1]  W. Sirignano,et al.  Unsteady, Spherically-Symmetric Flame Propagation Through Multicomponent Fuel Spray Clouds , 1991 .

[2]  S. Sazhin,et al.  Convective vaporization of a fuel droplet with thermal radiation absorption , 2006 .

[3]  L. Mees,et al.  Evaluation of temperature gradients within combusting droplets in linear stream using two colors laser-induced fluorescence , 2005 .

[4]  Sergei Sazhin,et al.  Droplet vaporization model in the presence of thermal radiation , 2005 .

[5]  G. Lavergne,et al.  Temperature measurements of binary droplets using three-color laser-induced fluorescence , 2006 .

[6]  S. Sazhin,et al.  Models for fuel droplet heating and evaporation: Comparative analysis , 2006 .

[7]  G. Faeth Evaporation and combustion of sprays , 1983 .

[8]  G. Thodos,et al.  Vapor-liquid equilibrium measurements for the ethanol-acetone system at 372.7, 397.7, and 422.6 K , 1987 .

[9]  U. Renz,et al.  Vaporization of a binary unsteady spray at high temperature and high pressure , 1994 .

[10]  G. Castanet,et al.  Bicomponent droplets evaporation: Temperature measurements and modelling , 2008 .

[11]  P. Lage,et al.  Nonideal vaporization of dilating binary droplets with radiation absorption , 1995 .

[12]  W. Sirignano,et al.  Multicomponent Transient Droplet Vaporization with Internal Circulation: Integral Equation Formulation and Approximate Solution , 1986 .

[13]  R. Reid,et al.  The Properties of Gases and Liquids , 1977 .

[14]  C. Maqua Contribution à la compréhension de l'évaporation de gouttes de combustible bi-composant à l'aide de méthodes optiques , 2007 .

[15]  S. Sazhin Advanced models of fuel droplet heating and evaporation , 2006 .

[16]  A. A. Amsden,et al.  Efficient multicomponent fuel algorithm , 2003 .

[17]  Rolf D. Reitz,et al.  Modeling of Multicomponent Fuels Using Continuous Distributions with Application to Droplet Evaporation and Sprays , 1997 .

[18]  A finite conductivity model for diesel spray evaporation computations , 1999 .

[19]  W. Sirignano,et al.  Fluid Dynamics and Transport of Droplets and Sprays , 1999 .

[20]  S. Sazhin,et al.  Monodisperse monocomponent fuel droplet heating and evaporation , 2010 .

[21]  Morgan Heikal,et al.  Transient heating of diesel fuel droplets , 2004 .

[22]  Rolf D. Reitz,et al.  A model for high-pressure vaporization of droplets of complex liquid mixtures using continuous thermodynamics , 2002 .

[23]  Sergei Sazhin,et al.  A Parabolic Temperature Profile Model for Heating of Droplets , 2003 .

[24]  G. G. Stokes "J." , 1890, The New Yale Book of Quotations.

[25]  G. Angelino,et al.  Modern Research Topics in Aerospace Propulsion , 1991 .

[26]  G. Thodos,et al.  Vapor—liquid equilibrium measurements for the methanol—acetone system at 372.8, 397.7 and 422.6 K , 1986 .

[27]  Sergei Sazhin,et al.  A simplified non-isothermal model for droplet heating and evaporation , 2003 .

[28]  Richard Weiss,et al.  Thermodynamics of the Liquid State , 1984 .

[29]  William A. Sirignano,et al.  Droplet vaporization model for spray combustion calculations , 1988 .

[30]  Morgan Heikal,et al.  New approaches to numerical modelling of droplet transient heating and evaporation , 2005 .

[31]  W. Hallett,et al.  A continuous thermodynamics model for multicomponent droplet vaporization , 1995 .

[32]  S. Sazhin,et al.  Monodisperse droplet heating and evaporation: experimental study and modelling , 2008 .

[33]  J. C. Jaeger,et al.  Conduction of Heat in Solids , 1952 .

[34]  Rainer Koch,et al.  Droplet evaporation modeling by the distillation curve model: accounting for kerosene fuel and elevated pressures , 2003 .

[35]  M. Orain,et al.  Investigation of heat and mass transfer between the two phases of an evaporating droplet stream using laser-induced fluorescence techniques: Comparison with modeling , 2007 .