Non-Isothermal Kinetic Modelling for Hydrogen Reduction of Ferric Oxide Using Matlab

Article Preview

Abstract:

Reduction of iron oxide by hydrogen is important in the production of direct reduced iron. This method of iron production is gaining increasing significance as an alternative route to the blast furnace technology with the many difficult issues facing the latter, the most important being the problem related to environmental. In order to reduce the emission of greenhouse gases CO2, particularly for iron making, the production of Direct Reduced Iron (DRI) using hydrogen as the reducing gas instead of carbon monoxide is being considered. Reduction of pure hematite by hydrogen was studied at the laboratory scale, varying the experimental conditions like temperature (700oC and 800oC) and porosity (20% and 40%). Then, a Kinetic Modelling was conducted using Matlab software based on independently measured physical and thermodynamic properties of the reaction system and experimentally measured properties of the reactant solid (Fe2O3), gas phase (H2) and reactant product (Fe). There is a gap that occurs between the predicted result and the experimental result although the model explicated the trend and the behaviour of the reduction rate of Ferric Oxide and indicated a good homogeneity to the experimental conditions used in this research.

You might also be interested in these eBooks

Info:

Periodical:

Pages:

3-8

Citation:

Online since:

June 2015

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2015 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

* - Corresponding Author

[1] Seetharaman, S. Fundamentals of Metallurgy, Woodhead Publishing and Maney Publishing (2005).

Google Scholar

[2] Li, Q. J. & Hong X. Non-isothermal kinetic model for reduction of ferrousoxide with hydrogen and carbon monoxide. Ironmaking & Steelmaking, (2009), 36(1), pp.24-28.

DOI: 10.1179/174328107x203787

Google Scholar

[3] Homma, S., S. Ogata, et al. Gas solid reaction model for a shrinking spherical particle with unreacted shrinking core. Chemical Engineering Science, (2005), 60(18), pp.4971-4980.

DOI: 10.1016/j.ces.2005.03.057

Google Scholar

[4] Abd Elhamid, M. H., M. M. Khader, et al. Autocatalytic Reduction of Hematite with Hydrogen under Conditions of Surface Control: A Vacancy-Based Mechanism. Journal of Solid State Chemistry, (1996), 123(2), pp.249-254.

DOI: 10.1006/jssc.1996.0175

Google Scholar

[5] Ronald C. G. , A Determination of the Transport-limited Reaction Rate for A Gas-Solid Reaction Forming a porous Reaction Product. PhD Dissertation, Lehigh University (1971).

Google Scholar

[6] Tan Weng Giap Kinetic Modelling For Hydrogen Reduction of Ferric Oxide Using Matlab. Degree of Bachelor Dissertation, School of Materials and Minerals Resources Engineering, Universiti Sains Malaysia, (2012), pp.1-104.

Google Scholar

[7] Constantineau, J. P. Modified predominance diagrams for gas-solid reactions. Metallurgical and Materials Transactions, (2000), 31(6), pp.1429-1437.

DOI: 10.1007/s11663-000-0027-x

Google Scholar