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Two phase flow modeling in circulating fluidized bed for different number of solid fractions and different geometry configurations

Wybrane pełne teksty z tego czasopisma
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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
Results of modeling of two phase gas-solid flow hydrodynamics in a fluidization column and column - cyclone - recirculation system are discussed in this study. A mathematical model is proposed implemented in FLUENT 6.2 commercial solver as well as in Kinetics Theory of Granular Flow. Simulation was carried out for several solid fractions. The influence is shown of an increased quantity of the solid fraction on stability circulation inside the column and external circulation in a complete system. Solid mass flux balance is presented in three characteristic points, and also the axial solid velocity distribution and solid volume fraction in the third characteristic column height. The proposed model predicts correctly the hydrodynamics of gas-solid flow in a circulating fluidized bed, with characteristic solid fluctuation and solid fraction distribution and velocity, observed also in a real laboratory column.
Rocznik
Strony
99--110
Opis fizyczny
Tab., wykr.,Bibliogr. 12 poz.,
Twórcy
autor
  • Politechnika Łódzka, Wydział Inżynierii Procesowej i Ochrony Środowiska, Katedra Systemów Inżynierii Środowiska, ul. Wólczańska 215, 93-005 Łódź
Bibliografia
  • [1] ENWALD H., PEIRANO E. AND ALMSTEDT A.E.: Eulerian two-phase flow theory applied to fluidization, Int. Multiphase Flow (1996) No. 22, 21-66.
  • [2] SUN B. AND GIDASPOW D.: Computation of circulating fluidized-bed riser how for the fiuidization VIII benchmark test, Ind. Eng. Chem. Res., Journal 38 (1999) No. 3, 787-792.
  • [3] VAN WACHEM B.G.M., SCHOUTEN J.C., KRISHNA R., VAN DEN BLEEK C.M.: Validation of the Eulerian simulated dynamic behaviour of gas-solid fluidised beds, Chem. Eng. Sci. (1999) No. 54, 2141-2149.
  • [4] IBSEN C.H., SOLBERG T., AND HJARTAGER B.H.: Evaluation of a three-dimensional numerical model of a scaled circulating fluidized bed, Ind. Eng. Chem. Res., Journal 40 (2001) N0. 23, 5081-5086.
  • [5] DING J., GIDASPOW D., A BUBBLING: Fluidization model using kinetic theory of granular flow, AIChE Journal, (1990), No. 36, 523-538.
  • [6] GIDASPOW D., BEZBURUAH R., AND DING J.: Hydrodynamics of circulating fluidized beds: kinetic theory approach, Proc. of the 7th Engineering Foundation Conference on Fluidization, 1992, 75-82.
  • [7] EASTWICK C.N., PICKERNG S.J., AROUSSI A.: Comparisons of two commercial computational fluid dynamics codes in modelling pulverised coal combustion for a 2.5 MW burner, Applied Math. Model., (1999) No. 23, 437-446.
  • [8] JOHANSEN S.T. AND LAUX H,: Simulation of granular materials flows, Proc. of RELPOWFLO III, Proc. of the Int. Symp. on the Reliable Flow of Particulate Solids, 11-13 August, Telemark College, Porsgrunn, Norway 1999.
  • [9] NAKAMURA K., CAPES, C.E.: Vertical pneumatic conveying - an experimental study with particles in the intermediate and turbulent flow regimes, Canadian J. of Chem. Eng., Journal 51 (1973), No. 2, 31-38.
  • [10] ANDERSON T.B., JACKSON R.: A Fluid mechanical description of fluidized beds: equations of motion, I & EC Fundam., (1967) No. 6, 527-539.
  • [11] SZAFRAN R.G.: Modelling of drying in a spouted bed dryer, Ph.D. Thesis, Wroclaw University of Technology, Institute of Chemical Engineering and Heating Equipment, 2004.
  • [12] BIS Z,: Circulating fluidization of mixture polydispersity materials, Technical University of Czestochowa 1999.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BGPK-1546-6150
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