OP-II-3

PP-I-29commercial CFD solver FLUENT. The simulation results are presented in a form ofspatial distributions of temperature, velocity, pressure, concentrations, particleaverage size in 2D tubular gas phase reactor. Comparison of simulation results withpreviously published data is given, and sensitivity of model predictions to the modelparameters is discussed.References[1]. Xiong, Y., Pratsinis, S. E. “Gas Phase Production of Particles in Reactive Turbulent Flows”,J. Aerosol Sci., (1991), 12, 637-655.[2]. Kolesnikov, A. V., Alexeev, N., Samokhin, A. "Controlled Synthesis of Alumina Nanoparticles in aReactor with Self-Impinging Plasma Jets" International Journal of Chemical Reactor Engineering,(2007) Vol. 5: A95.[3]. Gomez, A., Rosner, D. E. “Thermophoretic Effects on Particles in Counterflow Laminar DiffusionFlames “,Combustion Science and Technology, (1993), 89, 335 – 362.[4]. Pyykönen, J., Jokiniemi, J. “Model studies of deposition in turbulent boundary layer with inertialeffects”. Proceedings of the VIII Finnish National Aerosol Symposium. (2001) Report Series inAerosol Science 54, Finnish Association for Aerosol Research. 28−38.273