Abstract
Hydrogen plasma heating, a unique method for heating and reducing iron ore, is distinguished by its high heat, rapid reduction, and high efficiency, making it a promising technique in the metallurgy field. In this study, a non-transferred arc plasma heating system was used with Ar-H(2) as the working gas and acidic pellets as the raw material. The microstructures and elemental distributions of the slag and iron phases during the reduction process were examined using electron microscopy and energy-dispersive X-ray. The variation patterns of Fe-containing phases in the reduction products were found using X-ray diffraction and full-spectrum fitting refinement. The conversion rate of the oxidized pellets and the deoxidation conversion rate per area were estimated for various gas flow rates and reduction times. A reaction kinetics model was also used to study the reaction controlling step. The results showed that during the reduction process, with an H(2) flow rate of 4.5 L min(-1) and a 40 min reduction, the conversion(α) reached 99.89% and the purity of the reduced metallic iron reached 99.9%, achieving the industrial-grade 3N standard. Si and Al in the melt bath generated fayalite (Fe(2)SiO(4)) and hercynite (FeAl(2)O(4)) with Fe(x)O. The deoxidation conversion rate per unit area was 1.11 g (cm(2) min)(-1). A three-dimensional diffusion-controlled model was used to describe the reduction process, and the mechanism function was 2/3(1 + α)(3/2)[(1 + α)(1/3)](-1). The values of the reduction reaction rate constant (K) were 12.6 × 10(-2) s(-1) and 12.8 × 10(-2) s(-1) when the flow rates of H(2) gas were 3 and 4.5 L min(-1), respectively. The apparent activation energy was 21.9 kJ mol(-1). The empirical equation for the specific reduction rate was calculated as ln r = -2637.5/T - 0.407.