Gas-Solid Turbulent Flow in a Circulating Fluidized Bed Riser; Numerical Study of Binary Particle Mixtures

Y. He, N.G. Deen, M. van Sint Annaland, J.A.M. Kuipers

    Research output: Contribution to conferencePaperAcademic

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    Abstract

    A numerical simulation was performed on a turbulent gas-particle multi-phase flow in a circulating fluidized bed riser based on a hard-sphere discrete particle model (DPM) for the particle phase and the Navier-Stokes equations for the gas phase. The sub-grid scale stresses (SGS) were modeled with the SGS model proposed by Vreman (2004). The model enables the calculation of an arbitrary particle size distribution. In this work, binary mixtures of particles with different diameters are used in the simulation. From the numerical results it is found that the particles display a radial and axial diameter distribution. Small particles have a higher vertical particle velocity than the large particles. With increasing superficial gas velocity, the vertical particle velocity is increased. The average particle velocity and concentration vary both in the radial and axial directions. Finally, the numerical results are compared with the experimental and numerical results of Mathiesen et al (2000).
    Original languageEnglish
    Number of pages6
    Publication statusPublished - 2008
    Event9th International Conference on Circulating Fluidized Beds, CFB-9 2008 - Hamburg, Germany
    Duration: 13 May 200816 May 2008
    Conference number: 9

    Conference

    Conference9th International Conference on Circulating Fluidized Beds, CFB-9 2008
    Abbreviated titleCFB-9
    CountryGermany
    CityHamburg
    Period13/05/0816/05/08

    Fingerprint

    risers
    turbulent flow
    beds
    gases
    grids
    particle size distribution
    Navier-Stokes equation
    binary mixtures
    simulation
    vapor phases

    Keywords

    • IR-67406

    Cite this

    He, Y., Deen, N. G., van Sint Annaland, M., & Kuipers, J. A. M. (2008). Gas-Solid Turbulent Flow in a Circulating Fluidized Bed Riser; Numerical Study of Binary Particle Mixtures. Paper presented at 9th International Conference on Circulating Fluidized Beds, CFB-9 2008, Hamburg, Germany.
    He, Y. ; Deen, N.G. ; van Sint Annaland, M. ; Kuipers, J.A.M. / Gas-Solid Turbulent Flow in a Circulating Fluidized Bed Riser; Numerical Study of Binary Particle Mixtures. Paper presented at 9th International Conference on Circulating Fluidized Beds, CFB-9 2008, Hamburg, Germany.6 p.
    @conference{ff8e2e0ad627481682f15c8f594746bd,
    title = "Gas-Solid Turbulent Flow in a Circulating Fluidized Bed Riser; Numerical Study of Binary Particle Mixtures",
    abstract = "A numerical simulation was performed on a turbulent gas-particle multi-phase flow in a circulating fluidized bed riser based on a hard-sphere discrete particle model (DPM) for the particle phase and the Navier-Stokes equations for the gas phase. The sub-grid scale stresses (SGS) were modeled with the SGS model proposed by Vreman (2004). The model enables the calculation of an arbitrary particle size distribution. In this work, binary mixtures of particles with different diameters are used in the simulation. From the numerical results it is found that the particles display a radial and axial diameter distribution. Small particles have a higher vertical particle velocity than the large particles. With increasing superficial gas velocity, the vertical particle velocity is increased. The average particle velocity and concentration vary both in the radial and axial directions. Finally, the numerical results are compared with the experimental and numerical results of Mathiesen et al (2000).",
    keywords = "IR-67406",
    author = "Y. He and N.G. Deen and {van Sint Annaland}, M. and J.A.M. Kuipers",
    year = "2008",
    language = "English",
    note = "9th International Conference on Circulating Fluidized Beds, CFB-9 2008, CFB-9 ; Conference date: 13-05-2008 Through 16-05-2008",

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    He, Y, Deen, NG, van Sint Annaland, M & Kuipers, JAM 2008, 'Gas-Solid Turbulent Flow in a Circulating Fluidized Bed Riser; Numerical Study of Binary Particle Mixtures' Paper presented at 9th International Conference on Circulating Fluidized Beds, CFB-9 2008, Hamburg, Germany, 13/05/08 - 16/05/08, .

    Gas-Solid Turbulent Flow in a Circulating Fluidized Bed Riser; Numerical Study of Binary Particle Mixtures. / He, Y.; Deen, N.G.; van Sint Annaland, M.; Kuipers, J.A.M.

    2008. Paper presented at 9th International Conference on Circulating Fluidized Beds, CFB-9 2008, Hamburg, Germany.

    Research output: Contribution to conferencePaperAcademic

    TY - CONF

    T1 - Gas-Solid Turbulent Flow in a Circulating Fluidized Bed Riser; Numerical Study of Binary Particle Mixtures

    AU - He, Y.

    AU - Deen, N.G.

    AU - van Sint Annaland, M.

    AU - Kuipers, J.A.M.

    PY - 2008

    Y1 - 2008

    N2 - A numerical simulation was performed on a turbulent gas-particle multi-phase flow in a circulating fluidized bed riser based on a hard-sphere discrete particle model (DPM) for the particle phase and the Navier-Stokes equations for the gas phase. The sub-grid scale stresses (SGS) were modeled with the SGS model proposed by Vreman (2004). The model enables the calculation of an arbitrary particle size distribution. In this work, binary mixtures of particles with different diameters are used in the simulation. From the numerical results it is found that the particles display a radial and axial diameter distribution. Small particles have a higher vertical particle velocity than the large particles. With increasing superficial gas velocity, the vertical particle velocity is increased. The average particle velocity and concentration vary both in the radial and axial directions. Finally, the numerical results are compared with the experimental and numerical results of Mathiesen et al (2000).

    AB - A numerical simulation was performed on a turbulent gas-particle multi-phase flow in a circulating fluidized bed riser based on a hard-sphere discrete particle model (DPM) for the particle phase and the Navier-Stokes equations for the gas phase. The sub-grid scale stresses (SGS) were modeled with the SGS model proposed by Vreman (2004). The model enables the calculation of an arbitrary particle size distribution. In this work, binary mixtures of particles with different diameters are used in the simulation. From the numerical results it is found that the particles display a radial and axial diameter distribution. Small particles have a higher vertical particle velocity than the large particles. With increasing superficial gas velocity, the vertical particle velocity is increased. The average particle velocity and concentration vary both in the radial and axial directions. Finally, the numerical results are compared with the experimental and numerical results of Mathiesen et al (2000).

    KW - IR-67406

    M3 - Paper

    ER -

    He Y, Deen NG, van Sint Annaland M, Kuipers JAM. Gas-Solid Turbulent Flow in a Circulating Fluidized Bed Riser; Numerical Study of Binary Particle Mixtures. 2008. Paper presented at 9th International Conference on Circulating Fluidized Beds, CFB-9 2008, Hamburg, Germany.