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Total 23 records

    Two-dimensional CFD simulation of chemical reactions in tapered-in and tapered-out fluidized bed reactors

    , Article Advanced Powder Technology ; Volume 30, Issue 1 , 2019 , Pages 136-147 ; 09218831 (ISSN) Askaripour, H ; Molaei Dehkordi, A ; Sharif University of Technology
    Elsevier B.V  2019
    Abstract
    This article presents a simulation study of tapered-in and tapered-out fluidized bed reactors to investigate the influences of apex angle on the fractional conversion and the pressure drop of the fluidized beds in the presence of two types of chemical reaction with gas volume increase and reduction. The 2D behavior of tapered-in and -out fluidized beds was also compared with a columnar one from fractional conversion and bed pressure drop point of views. To validate the simulation results, the numerical predictions for the expansion ratio and the pressure drop of a tapered fluidized bed were compared with experimental data and good agreement was observed. The obtained simulation results... 

    Optimum operating conditions for direct oxidation of h 2s in a fluidized bed reactor

    , Article World Academy of Science, Engineering and Technology ; Volume 79 , 2011 , Pages 237-241 ; 2010376X (ISSN) Golestani, F ; Kazemeini, M ; Fattahi, M ; Amjadian, A ; Sharif University of Technology
    2011
    Abstract
    In this research a mathematical model for direct oxidization of hydrogen sulfide into elemental sulfur in a fluidized bed reactor with external circulation was developed. As the catalyst is deactivated in the fluidized bed, it might be placed in a reduction tank in order to remove sulfur through heating above its dew point. The reactor model demonstrated via MATLAB software. It was shown that variations of H 2S conversion as well as; products formed were reasonable in comparison with corresponding results of a fixed bed reactor. Through analyzing results of this model, it became possible to propose the main optimized operating conditions for the process considered. These conditions included;... 

    Steam reforming of methane in a tapered membrane - Assisted fluidized - Bed reactor: Modeling and simulation

    , Article International Journal of Hydrogen Energy ; Volume 36, Issue 1 , 2011 , Pages 490-504 ; 03603199 (ISSN) Dehkordi, A. M ; Savari, C ; Ghasemi, M ; Sharif University of Technology
    Abstract
    A compartment model was developed to describe the flow pattern of gas within the dense zone of a tapered membrane-assisted fluidized-bed reactor (TMAFBR), in the bubbling mode of operation for steam reforming of methane under wall heat flux. The parameters of the developed model (i.e., number of compartments for the bubble and emulsion phases) were determined using the experimental data reported elsewhere [Adris AM, Lim CJ, Grace JR. The fluidized bed membrane reactor system: a pilot scale experimental study. Chem Eng Sci 1994; 49:5833-43.] and good agreements were obtained between model predictions and corresponding experimental data. The developed model was then utilized to predict the...