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Instability of the interface between fluids of different densities flowing through a complex vertical hydraulic system

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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
The impact of the gas density difference on formation of flow patterns of fluids of different density was analysed. Physical modelling of a non-isothermal laminar flow of a gas mixture in a vertical epitaxial reactor chamber was carried out and the model flow was visualised. Visualisation studies, performed using a smoke method, confirmed that the stability of a gas interface determines the flow pattern in the chamber. The Rayleigh-Taylor instability occurs in the flow through a reactor, which, together with the Kelvin-Helmholtz instability and with the superposition of convection flows on the principal flow, shapes the flow pattern in the whole reactor chamber. On the basis of results of visualisation studies, the possibility of making the flow through a vertical reactor stable was indicated if the inlet guide apparatus is applied and the flow direction is reversed.
Rocznik
Strony
403--411
Opis fizyczny
Bibliogr. 18 poz., rys.
Twórcy
autor
  • Faculty of Mechanical and Power Engineering, Wrocław University of Technology Wybrzeże Wyspiańskiego 27, 50-370 Wrocław, POLAND
  • Faculty of Mechanical and Power Engineering, Wrocław University of Technology Wybrzeże Wyspiańskiego 27, 50-370 Wrocław, POLAND
autor
  • Faculty of Mechanical and Power Engineering, Wrocław University of Technology Wybrzeże Wyspiańskiego 27, 50-370 Wrocław, POLAND
Bibliografia
  • [1] Andrews MJ. and Spalding D.B. (1991): A simple experiment to investigate two-dimensional mixing by Rayleigh- Taylor instability. - preprint, Phys. Fluids.
  • [2] Baker L. (1986): Rayleigh-Taylor instability, In: Encyklopedia of Fluid Mechanics. - Houston, London, Paris, Tokyo: Gulf Publishing Company, vol.l.
  • [3] Book D.L. (1986): Rayleigh-Taylor instability in compressible media, In: Encyklopedia of Fluid Mechanics. - Houston, London, PuriN, Tokyo: Gulf Publishing Company, vol.l.
  • [4] Goldstein R, (1983): Fluid Mechanics Measurements. - Washington, New York, London: Hemisphere Publishing Corporation.
  • [5] Grygoriev A., Jeżowiecka-Kabsch K. and Szewczyk H. (2001): Modelling of flow through the vertical OMVPE reactor. - Chem. Proc. Enging., vol.22, pp.505-525 (in Polish).
  • [6] Idelćik I.E. (1982): Some interesting phenomena and paradoxes of aerodynamic and hydraulic. - Moskva: Masinostroenie.
  • [7] Jensen K.F. (1989): Transport phenomena and Chemical reaction issues in OMVPE of compound semiconductors. - Journal of Crystal Growth, vol.98, pp.148-166.
  • [8] Jeżowiecka-Kabsch K., Szewczyk H., Grygoriev A., Tłaczała M., Panek M. and Korbutowicz R. (1996): Modelling of non-isothermal flow through OMVPE reactor. - XII-th National Conference on Fluid Mechanics, Rzeszów, vol 2 pp.241-248 (in Polish).
  • [9] Jeżowiecka-Kabsch K., Szewczyk H., Grygoriev A., Tłaczała M., Panek M. and Korbutowicz R. (1996): Flow visualisation studies for the non-isothermal model of OMVPE. - XII-th National Conference on Fluid Mechanics, Rzeszów, vol.2, pp.249-256 (in Polish).
  • [10] Jurgensen H. (1992): Large-scale MOVPE production systems. - Microelectronic Engineering, vol,18, pp.l 19-148.
  • [11] Kudela H. (1995): Numerical Modelling of the Hydrodynamic Phenomena by the Vortex Methods. - Reports of the Institute of Heat Engineering, Technical University of Wrocław, Monographs No.25, Wrocław, p.120 (in Polish).
  • [12] Merzkirch W. (1987): Flow Vizualisation. - Orlando, New York, London: Academic Press.
  • [13] Pan T.W., Joseph D.D. and Głowiński R. (2001): Modelling Rayleigh-Taylor instability of sedimenting suspension of several thousand circular particles in a direct numerical simulation. - Journal of Fluid Mechanics, vol 434 pp.23-37.
  • [14] Razeghi M. (1989): The MOCVD Challenge. - Bristol: IOP Publishing Ltd, vol.l.
  • [15] Read K.I. (1984): Experimental investigation of turbulent mixing by Rayleigh-Taylor instability. - Physica D, vol.l2, pp.45-58.
  • [16] Szewczyk H., Jeżowiecka-Kabsch K. and Grygoriev A. (2001): The non-isothermal flow pattern in a complex hydraulic system. - First International Conference of Fluid Structure Interaction, Halkidiki, vol. 1, pp.223-232.
  • [17] Taylor G.I. (1950): The instability of liquid surfaces when accelerated in a direction perpendicular to their planes. - Proc. R. Soc. London Ser., vol.A201, pp.192-196.
  • [18] Wang C.A., Groves S.H., Palmateer S.C., Weyburne D.W. and Brown R.A. (1983): Flow visualization studies for optimization of OMVPE reactor desing. - Journal of Crystal Growth, vol.92, pp.l76-184.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BPZ2-0003-0017
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