4.7 Article

Reduction and oxidation kinetics of different phases of iron oxides

Journal

INTERNATIONAL JOURNAL OF HYDROGEN ENERGY
Volume 40, Issue 6, Pages 2613-2620

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ijhydene.2014.12.099

Keywords

Iron ores; Redox reactions; Kinetics; Iron oxide phases; Hydrogen production; Chemical looping process

Funding

  1. Industrial Source Technology Development Programs of the Ministry of Knowledge Economy (MKE) of Korea [2013-10042712]
  2. National Research Foundation of Korea (NRF) - Korea government [NRF-2014R1A1A2A16055557]
  3. R&D Center for Valuable Recycling (Global-Top R&D Program) of the Ministry of Environment [GT-14-C-01-038-0]
  4. POSCO [POSCO-2014X027]

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The redox properties and kinetic parameters of three different phases of as-received iron ores such as gamma-FeOOH, Fe2O3, and Fe3O4 were investigated using isothermal experiments for reduction and oxidation reaction using hydrogen and H2O, respectively, to investigate the possibility for chemical looping process to produce pure hydrogen. Among the selected kinetic equations of three different iron oxide ores for the reduction at 800 degrees C and oxidation in the temperature ranges 700-850 degrees C, three-dimensional diffusion kinetic model such as Jander equation was well fitted with the experimental redox reactions of the three different iron ores. The calculated activation energies of iron ores with a main phase of gamma-FeOOH, Fe2O3, and Fe3O4, for the oxidation reaction with H2O, were found to be around 21.5, 48.9, and 11.0 kJ/mol, respectively. The smaller activation energy and larger oxidation rate were observed on the Fe3O4 phase iron ore owing to its large reduction rate and stable particle size maintenance even under high temperature redox reactions, and it is suitable for the further application to chemical looping process. Copyright (C) 2014, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.

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