PL EN


Preferencje help
Widoczny [Schowaj] Abstrakt
Liczba wyników
Tytuł artykułu

Numerical simulation of thermal-hydraulic processes in the riser chamber of installation for clinker production

Treść / Zawartość
Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
Clinker burning process has a decisive influence on energy consumption and the cost of cement production. A new problem is to use the process of decarbonization of alternative fuels from waste. These issues are particularly important in the introduction of a two-stage combustion of fuel in a rotary kiln without the typical reactor-decarbonizator. This work presents results of numerical studies on thermal-hydraulic phenomena in the riser chamber, which will be designed to burn fuel in the system where combustion air is supplied separately from the clinker cooler. The mathematical model is based on a combination of two methods of motion description: Euler description for the gas phase and Lagrange description for particles. Heat transfer between particles of raw material and gas was added to the numerical calculations. The main aim of the research was finding the correct fractional distribution of particles. For assumed particle distribution on the first stage of work, authors noted that all particles were carried away by the upper outlet to the preheater tower, what is not corresponding to the results of experimental studies. The obtained results of calculations can be the basis for further optimization of the design and operating conditions in the riser chamber with the implementation of the system.
Rocznik
Strony
127--142
Opis fizyczny
Bibliogr. 21 poz., rys., tab., wz.
Twórcy
autor
  • Opole University of Technology, Department of Thermal Engineering and Industrial Facilities,Prószkowska 76, 45-758 Opole, Poland
  • Opole University of Technology, Department of Thermal Engineering and Industrial Facilities,Prószkowska 76, 45-758 Opole, Poland
  • Opole University of Technology, Department of Thermal Engineering and Industrial Facilities,Prószkowska 76, 45-758 Opole, Poland
autor
  • Opole University of Technology, Department of Thermal Engineering and Industrial Facilities,Prószkowska 76, 45-758 Opole, Poland
autor
  • Opole University of Technology,Department of Innovative Processes, Prószkowska 76, 45-758 Opole, Poland
Bibliografia
  • [1] Saidura R., Hossaina M.S., Islama M.R., Fayazb H., Mohammed H.A.: A review on kiln system modeling. Renew. Sust. Energ. Rev. 15(2011), 5, 2487–2500.
  • [2] Fidaros D.K., Baxevanou C.A., Dritselis C.D., Vlachos N.S.: Numerical modelling of flow and transport processes in a calciner for cement production. Powder Technol. 171(2007), 2, 81–95.
  • [3] Hu Z., Lu J., Huang L., Wang S.: Numerical simulation study on gas-solid twophase flow in pre-calciner. Commun. Nonlinear Sci. 11(2006), 3, 440–451.
  • [4] Stoyan D., Wuibull: RRSB or extreme-value theorists? Metrika, 76(2013), 2, 153–159.
  • [5] Apte S.V., Maheshy K., Lundgrenz T.: A Eulerian-Lagrangian model to simulate two-phase/particulate flows. In: Center for Turbulence Research, Annual Research Briefs (2003), 161–171.
  • [6] Kosinski P., Kosinska A., Hoffmann A.C.: Fluid-particle flows in a driven cavity. In: Proc. Int. Conf. of Numerical Analysis and Applied Mathematics ICNAAM – 2006, 1–4.
  • [7] Kosinski P., Hoffmann A.C.: An extension of the hard-sphere particle-particle collision model to study agglomeration. Chem. Eng. Sci. 65(2010), 10, 3231–3239.
  • [8] Widhalm M.: Lagrangian trajectory simulation of rotating regular shaped ice particles. SAE Tech. Paper 2015-01-2141, 2015, doi:10.4271/2015-01-2141.
  • [9] Wydrych J., Borsuk G., Dobrowolski B., G.Nowosielski: Numerical modelling of gas-particle countercurrent flow in the installation for clinker production. In: Proc. 8th Int. Conf. on Inverse Problems in Engineering, 12-15 May 2014, Kraków.
  • [10] Borsuk G, Dobrowolski B. Wydrych, J.: Gas-solids mixture flow through a two-bend system. Chem. Process Eng. 27(2006), 3/1, 645–656.
  • [11] Wydrych J.: Comparative analysis of the methods of simulation of flow in boiler dust systems. Chem. Process Eng. 31(2010), 4, 603–623.
  • [12] Fidaros D.K., Baxevanou C.A., Dritselis C.D., Vlachos N.S.: Numerical modelling of flow and transport processes in a calciner for cement production. Powder Technol. 171(2007), 2, 81–95.
  • [13] Krysiński T., Buliński Z., Nowak A.J.: Numerical modeling and preliminary validation of drag-based vertical axis wind turbine. Arch. Thermodyn. 36(2015), 1, 19–38.
  • [14] Mujumdara K.S., Ganesha K.V., Kulkarnia S.B., Ranade V.V.: Rotary Cement Kiln Simulator (RoCKS): Integrated modeling of pre-heater, calciner, kiln and clinker cooler. Chem. Eng. Sci. 62(2007), 9, 2590–2607.
  • [15] Göbel F., Mundt C.: Implementation of the P1 radiation model in the CFD solver NSMB and investigation of radiative heat transfer in the SSME main combustion chamber. In: Proc. 17th AIAA Int. Space Planes and Hypersonic Systems and Technologies Conference, (2011).
  • [16] Mikulcic H., von Berg E., Vujanovic M., Priesching P., Perkovic L., Tatschl R., Duic N.: Numerical modeling of calcinations reaction mechanism for cement production. Chem. Eng. Sci. 69(2012), 1, 607–615.
  • [17] ANSYS Fluent, Release 14.0, ANSYS Inc.
  • [18] Bilirgen H., Levy E.K.: Mixing and dispersion of particle ropes in lean phase pneumatic conveying. Powder Technol. 119(2001), 2-3, 134–152.
  • [19] Yilmaz A., Levy E.K.: Formation and dispersion of ropes in pneumatic conveying. Powder Technol. 114(2001), 1-3, 168–185.
  • [20] Wardach-Święcicka I., Kardaś D.: Modeling of heat and mass transfer during thermal decomposition of a single solid fuel particle. Arch. Thermodyn. 34(2013), 2, 53–71.
  • [21] Krawczyk P., Badyda K.: Two-dimensional CFD modeling of the heat and mass transfer process during sewage sludge drying in a solar dryer. Arch. Thermodyn. 32(2011), 4, 3–16.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-179d0061-f1bf-4e97-92af-60ed9fa9c832
JavaScript jest wyłączony w Twojej przeglądarce internetowej. Włącz go, a następnie odśwież stronę, aby móc w pełni z niej korzystać.