Article ID Journal Published Year Pages File Type
672844 Thermochimica Acta 2015 10 Pages PDF
Abstract
Ferrous sulfate waste has become a bottleneck in the sustainable development of the titanium dioxide industry in China. In this study, we propose a new method for the reductive decomposition of ferrous sulfate waste using pyrite. Thermodynamics analysis, tubular reactor experiments, and kinetics analysis were performed to analyze the reaction process. The results of the thermodynamic simulation showed that the reaction process and products were different when molar ratio of FeSO4/FeS2 was changed. The suitable molar ratio of FeSO4/FeS2 was 8-12. The reaction temperature of ferrous sulfate with pyrite was 580-770 K and the main products were Fe3O4 and SO2. The simulation results agreed well with the experimental results. The desulphurization rate reached 98.55% and main solid products were Fe3O4 at 823.15 K when mole ratio of FeSO4/FeS2 was 8. Nano-sized magnetite was obtained at this condition. The kinetic model was investigated by isoconversional methods. The average E value was 244.34 kJ mol−1. The ferrous sulfate decomposition process can be treated as autocatalytic reaction mechanism, which corresponded to the expanded Prout-Tompson (Bna) model. The reaction mechanism of autocatalytic reactions during the process of ferrous sulfate decomposition were explored, the products of Fe oxide substances are the catalyst components.
Related Topics
Physical Sciences and Engineering Chemical Engineering Fluid Flow and Transfer Processes
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