Fray Symposium - Mathematical Modeling Of Fluidized-Bed Reactors Used In Non-Catalytic Gas-Solid Reactions
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2011-Sustainable Industrial Processing Summit
SIPS2011 Volume 1: Sustainable Non-ferrous Smelting in 21st Century

Editors:Florian K
Publisher:Flogen Star OUTREACH
Publication Year:2012
Pages:828 pages
ISBN:978-0-9879917-0-6
ISSN:2291-1227 (Metals and Materials Processing in a Clean Environment Series)

    Mathematical Modeling Of Fluidized-Bed Reactors Used In Non-Catalytic Gas-Solid Reactions

    Behnam Khoshandam1; Samaneh Maroufi1; Ramachandran Kumar2;
    1SEMNAN UNIVERSITY, Semnan, Iran; 2UNIVERSITY OF CAMBRIDGE, Cambridge, United Kingdom;
    Type of Paper: Invite
    Id Paper: 72
    Topic: 4

    Abstract:

    Mathematical modelling of a continuous fluidized-bed reactor has been carried out for non-catalytic gas–solid reactions. The two-phase bubblingbed model has been used. The feed stream size distribution with reversible or irreversible first-order kinetics can be considered by the model. The Grain model was used for non-catalytic reduction of solid reactants. A program was developed in MATLAB software for solving the governing equations at conditions of differenttemperatures and pressures. The model was validated using experimental data and simulation results available in the literature for the iron orereduction with a gas mixture containing hydrogen and was also used for predicting the extent of reaction for reduction of cobalt oxide by methane.

    Keywords:

    fluidized-bed reactor, mathematical modelling, reduction, iron ore, cobalt oxide

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    Cite this article as:

    Khoshandam B, Maroufi S, Kumar R. Mathematical Modeling Of Fluidized-Bed Reactors Used In Non-Catalytic Gas-Solid Reactions. In: Florian K, editors. Sustainable Industrial Processing Summit SIPS2011 Volume 1: Sustainable Non-ferrous Smelting in 21st Century. Volume 1. Montreal(Canada): FLOGEN Star Outreach;2012. p..