<p>In this work, a production process is proposed that uses high-volatile lignite coal to perform carbon‒hydrogen composite reduction of vanadium‒titanium magnetite (VTM) in response to the current trend of low carbon and green development in the steel industry. The reduction sequence and degree of lignite for VTM in a rotary kiln were analyzed using a stoichiometric model, a minimum free energy model, and thermogravimetric/differential scanning calorimetry (TG-DSC) experiments. The results indicate that 1000&#xa0;g of VTM requires 0.748&#xa0;Nm<sup>3</sup> of air and 445&#xa0;g of lignite coal (equilibrium system 1) or 487&#xa0;g of lignite coal (equilibrium system 2) for reduction, with H<sub>2</sub> contributing to approximately 11% of the reduction. The influence of gangue on the reduction process of VTM was also examined, revealing that the presence of CaO and MgO promotes Fe reduction, while Al<sub>2</sub>O<sub>3</sub> inhibits Fe reduction, and SiO<sub>2</sub> has minimal impact. Additionally, the reduction sequence of iron oxides was determined to be Fe<sub>2</sub>O<sub>3</sub> → FeSiO<sub>3</sub> → MgFe<sub>2</sub>O<sub>4</sub> → Fe<sub>3</sub>O<sub>4</sub> → FeO → Fe<sub>2</sub>SiO<sub>4</sub> → Fe<sub>2</sub>TiO<sub>4</sub> → FeTiO<sub>3</sub> → FeTi<sub>2</sub>O<sub>5</sub> → FeV<sub>2</sub>O<sub>4</sub> → FeAl<sub>2</sub>O<sub>4</sub>. Finally, TG-DSC experiments were used to verify the reduction process of the VTM. This work provides a clear description of the reduction process of VTM and elucidates the essence of carbon‒hydrogen composite reduction.</p>

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Thermodynamic analysis of the reduction of vanadium–titanium magnetite by a hydrocarbon composite from lignite

  • Wei-yang Zhang,
  • Han-jie Guo,
  • Shu-sen Cheng,
  • Jing Guo

摘要

In this work, a production process is proposed that uses high-volatile lignite coal to perform carbon‒hydrogen composite reduction of vanadium‒titanium magnetite (VTM) in response to the current trend of low carbon and green development in the steel industry. The reduction sequence and degree of lignite for VTM in a rotary kiln were analyzed using a stoichiometric model, a minimum free energy model, and thermogravimetric/differential scanning calorimetry (TG-DSC) experiments. The results indicate that 1000 g of VTM requires 0.748 Nm3 of air and 445 g of lignite coal (equilibrium system 1) or 487 g of lignite coal (equilibrium system 2) for reduction, with H2 contributing to approximately 11% of the reduction. The influence of gangue on the reduction process of VTM was also examined, revealing that the presence of CaO and MgO promotes Fe reduction, while Al2O3 inhibits Fe reduction, and SiO2 has minimal impact. Additionally, the reduction sequence of iron oxides was determined to be Fe2O3 → FeSiO3 → MgFe2O4 → Fe3O4 → FeO → Fe2SiO4 → Fe2TiO4 → FeTiO3 → FeTi2O5 → FeV2O4 → FeAl2O4. Finally, TG-DSC experiments were used to verify the reduction process of the VTM. This work provides a clear description of the reduction process of VTM and elucidates the essence of carbon‒hydrogen composite reduction.