Modeling and Simulation of Isothermal Reduction of a Single Hematite Pellet in Gas Mixtures of H2 and CO
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Ragnhild E. Aune | Reza Beheshti | John Moosberg-Bustnes | R. Aune | R. Beheshti | J. Moosberg-Bustnes | John Moosberg-Bustnes
[1] Hassan Hashemipour Rafsanjani,et al. Modeling and Simulation of Noncatalytic Gas-Solid Reaction in a Moving Bed Reactor , 2008 .
[2] Abdelhamid Ajbar,et al. Modelling and parametric studies of direct reduction reactor , 2011 .
[3] H. Ale Ebrahim,et al. Simulation of direct reduction reactor by the grain model , 2011 .
[4] E. T. Turkdogan,et al. Catalytic effect of iron on decomposition of carbon monoxide: I. carbon deposition in H2-CO Mixtures , 1974, Metallurgical and Materials Transactions B.
[5] M. Valipour. MATHEMATICAL MODELING OF A NON-CATALYTIC GAS-SOLID REACTION: HEMATITE PELLET REDUCTION WITH SYNGAS , 2009 .
[6] A. Rahimi,et al. A general model for moving-bed reactors with multiple chemical reactions, Part II: Effect of kinetic model , 2013 .
[7] Davide Manca,et al. Synchronizing Field and Control-Room Operators for Process Operating Transients , 2008 .
[8] J. Szekely,et al. A structural model for gas-solid reactions with a moving boundary-II: The effect of grain size, porosity and temperature on the reaction of porous pellets , 1971 .
[9] H. Sohn,et al. 7 – The kinetics of metallurgical reactions , 2005 .
[10] K. Chou,et al. Reduction Kinetics of Metal Oxides by Hydrogen , 2013 .
[11] D. Parisi,et al. Modeling of counter current moving bed gas-solid reactor used in direct reduction of iron ore , 2004 .
[12] B. Khoshandam,et al. Modelling of non-catalytic gas–solid reactions – multicomponent non-equimolar counter diffusion of gaseous phase , 2009 .
[13] L. Kolbeinsen. Modelling of DRI Processes with Two Simultaneously Active Reducing Gases , 2010 .
[14] T. Usui,et al. Analysis of rate of hydrogen reduction of porous wustite pellets basing on zone-reaction models. , 1990 .
[15] R. M. Smailer,et al. Direct reduced iron : technology and economics of production and use , 1980 .
[16] Y. Saboohi,et al. Mathematical modeling of the reaction in an iron ore pellet using a mixture of hydrogen, water vapor, carbon monoxide and carbon dioxide: an isothermal study , 2006 .
[17] Ivan Fořt. Comments to “CFD simulation of stirred tanks: Comparison of turbulence models. Part I: Radial flow impellers” and “Part II: Axial flow impellers, multiple impellers and multiphase dispersions” , 2012 .
[18] J. Szekely,et al. The influence of carbon deposition on the reduction kinetics of commercial grade hematite pellets with CO, H2, and N2 , 1983 .
[19] Abdelhamid Ajbar,et al. Modelling the complex interactions between reformer and reduction furnace in a midrex‐based iron plant , 2012 .