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    Compartment model for steam reforming of methane in a membrane-assisted bubbling fluidized-bed reactor

    , Article International Journal of Hydrogen Energy ; Volume 34, Issue 3 , 2009 , Pages 1275-1291 ; 03603199 (ISSN) Dehkordi, A.M ; Memari, M ; Sharif University of Technology
    2009
    Abstract
    A compartment model was developed to describe the flow pattern of gas within the dense zone of a membrane-assisted fluidized-bed reactor (MAFBR), in the bubbling mode of operation for steam reforming of methane both with (adiabatic) and without (isothermal) entering oxygen. Considering such a flow pattern and using the experimental data reported elsewhere [Roy S, Pruden BB, Adris AM, Grace JR, Lim CJ. Fluidized-bed steam methane reforming with oxygen input. Chem Eng Sci 1999; 54:2095-2102.], the parameters of the developed model (i.e., number of compartments for the bubble and emulsion phases) were determined and fair agreements were obtained between model predictions and experimental data.... 

    Operation of an industrial steam reformer under severe condition: a simulation study

    , Article Canadian Journal of Chemical Engineering ; Volume 86, Issue 4 , 29 July , 2008 , Pages 747-755 ; 00084034 (ISSN) Shayegan, J ; Motamed Hashemi, M. M. Y ; Vakhshouri, K ; Sharif University of Technology
    2008
    Abstract
    A rigorous two-dimensional model is developed for simulating the operation of a less-investigated type steam reformer having a considerably lower operating Reynolds number, higher tube diameter, and non-availability of extra steam in the feed compared with conventional steam reformers. Simulation results show that reasonable predictions can only be achieved when certain correlations for wall to fluid heat transfer equations are applied. In all cases, strong radial temperature gradients inside the reformer tubes have been found. Furthermore, the results show how a certain catalyst loading profile will affect the operation of the reformer. © 2008 Canadian Society for Chemical Engineering  

    Retrofitting a steam power cycle by using water from the interstage feed water pump as reheat spray

    , Article ASME Power Conference 2008, Lake Buena Vista, FL, 22 July 2008 through 24 July 2008 ; July , 2008 , Pages 23-30 ; 9780791848326 (ISBN) Saeedi, M. H ; Irani Rahaghi, A ; Mousavi, M. S ; Power Division, ASME ; Sharif University of Technology
    2008
    Abstract
    Various methods are used in thermal power plants to adjust the superheated or reheated steam temperature to a pre-determined set point, including flue gas recirculation, using tilting burners and spray of water from discharge of feed water pump, etc. In this paper, an innovative method is presented to control the reheater temperature by tapping water from an interstage of the feed water pump to control reheater temperature at the Bisotoun Power Plant (a steam cycle based power plant in the western Iran). The spray water for the superheaters is secured from the discharge of feed water pump, but interstage water, instead of gas recirculation or using tilting burner, is used to control the... 

    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... 

    Thermodynamic optimization of design variables and heat exchangers layout in HRSGs for CCGT, using genetic algorithm

    , Article Applied Thermal Engineering ; Volume 29, Issue 2-3 , 2009 , Pages 290-299 ; 13594311 (ISSN) Mohagheghi, M ; Shayegan, J ; Sharif University of Technology
    2009
    Abstract
    The heat recovery steam generator (HRSG) is one of the few equipments that are custom made for combined cycle power plants, and any change in its design affects all performance parameters of a steam cycle directly. Thus providing an optimization tool to optimize its design parameters and the layout of its heat exchangers is of great importance. A new method is introduced for modeling a steam cycle in advanced combined cycles by organizing non-linear equations and their simultaneous solutions by use of the hybrid Newton methods in this article. Thereafter, optimal thermodynamic performance conditions for HRSGs are calculated with the help of the genetic algorithm. In the conclusion, the... 

    Economic feasibility of CO2 capture from oxy-fuel power plants considering enhanced oil recovery revenues

    , Article Energy Procedia, 19 September 2010 through 23 September 2010 ; Volume 4 , September , 2011 , Pages 1886-1892 ; 18766102 (ISSN) Khorshidi, Z ; Soltanieh, M ; Saboohia, Y ; Arab, M ; Sharif University of Technology
    2011
    Abstract
    Considering the dramatic increase of greenhouse gases concentration in the atmosphere, especially carbon dioxide, reduction of these gases seems necessary to combat global warming. Fossil fuel power plants are one of the main sources of CO2 emission and several methods are under development to capture CO2 from power plants. In this paper, CO2 capture from a natural gas fired steam cycle power plant using oxyfuel combustion technology is studied. Oxy-fuel combustion is an interesting option since CO2 concentration in the flue gas is highly increased. The Integrated Environmental Control Model (IECM) developed by Carnegie Mellon University (USA) is used to evaluate the effect of this capture...