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    Experimental and Computaional Study of Compartmented Fluidized Bed Gasifier (CFBG)

    Access Status
    Fulltext not available
    Authors
    Wee, Siaw
    Chok, Vui
    Gorin, Alexander
    Chua, Han
    Date
    2008
    Type
    Conference Paper
    
    Metadata
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    Citation
    Wee, Siaw and Chok, Vui and Gorin, Alexander and Chua, Han. 2008. Experimental and Computaional Study of Compartmented Fluidized Bed Gasifier (CFBG), in HiTACG 2008, Jan 13 2008.Phuket, Thailand
    Source Title
    7th High Temprature Air Combustion and Gasfication International Symposium
    Source Conference
    HiTACG 2008
    Faculty
    Faculty Office
    Curtin Sarawak
    School
    Curtin Sarawak - Faculty Office
    URI
    http://hdl.handle.net/20.500.11937/18089
    Collection
    • Curtin Research Publications
    Abstract

    A pilot scale (0.5 tones/day) air-blown compartmented fluidized bed gasifier (CFBG) consisting of two compartments, the combustor and the gasifier, operating at bubbling fluidized mode has been constructed for medium calorific value syngas (>11 MJ/Nm3) production from biomass. The hydrodynamics of CFBG is studied experimentally and computationally. The experiments are carried out in a custom-made transparent CFBG cold model. The computational fluid dynamics (CFD) software, FLUENT, is employed in modeling the fluidized bed containing monodispersed size Geldart B particles, river sand, of 272 ?m and 2620 kg/m3 in diameter and density respectively. A three-dimensional Eulerian-eulerian granular model with closure laws according to the kinetic theory of granular flow is chosen to simulate the multiphase environs at 0.2 ? 3.2 Umf.The CFD simulated results show reasonably well agreement with experimental results in terms of bed pressure drop, bed expansion ratio and minimum fluidization velocity. The experimentally determined average fluidization quality over the operating bed height range is approximately 0.8.

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