147 publications from this institution
Pure Fe2O3 particles were coated with MgO using coprecipitation method under different conditions. For the aim of improving the coating amount and uniformity, the coprecipitation coating method was firstly studied to avoid sticking during fluidized reduction of iron ore. The actual coating amount on the particle surface was quantitatively determined, the sticking problem during fluidizing reduction can be avoided with a MgO coating amount around 0.411wt.%. The coating amount of MgO on the particle did not decrease after fluidized reduction. Samples were analyzed using (SEM/EDS) analysis, it was found that the MgO coating was effective and intact and merely no exposed part on the Fe2O3 particle surface. The coating uniformity was improved comparing to other coating methods. Precipitates of different crystal structures and morphology generated with different precipitation conditions tend to nucleated at the bottom part of the Fe2O3 particle as the nucleation energy there is lower.
As an environmentally hazardous waste, electric arc furnace (EAF) dust had a potential to provide a wider resource of potassium if recycled due to high potassium content. In this study, the chemical and mineralogical characteristics of the EAF dust, especially the existing state of potassium, were analyzed. The results showed that the dust consisted dominantly of manganese oxides (Mn3O4, MnO, MnO2) and manganese silicate (MnSiO3). The K element existed in the dust was in the form of potassium permanganate (K2Mn4O8, insoluble) and potassium sulfate/sulfite (soluble). Then the soluble potassium salts in the dust were recovered by water leaching and crystallization. The recovery ratio of K reached 88.2%, and the products K2SO4 and KCl with the K2O content of 65.25% were obtained. During leaching, the Mn3+ and Mn4+ components were reduced to Mn2+ by sulfide (S2−) or sulfite (SO32−), and the S2− and SO32− components were oxidized to SO42−. The leaching kinetics was studied by the specific electrical conductivity method. The apparent activation energy was 7.76±0.65 kJ/mol, suggesting that the rate controlling step of leaching process was the diffusion of K+ through the diffusion layer.