Thermodynamics of the MnO-FeO-MnS-FeS-SiO2 system at SiO 2 saturation under reducing condition: Immiscibility in the liquid phase

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Abstract

Phase Equilibria in the MnO-FeO-MnS-FeS-SiO2 liquid phase at SiO2 saturation under reducing condition were experimentally investigated in the temperature range from 1 200°C to 1 400°C in order to provide a fundamental knowledge on new FerroManganese (FeMn) alloy process. High temperature equilibration, quenching and Electron Probe Micro-Analysis (EPMA) were employed to obtain equilibrium compositions of liquid phase which was separated into oxide-rich liquid and sulfide-rich liquid. Concentration of Mn defined as RMn = nMn/nFe + n Mn in the sulfide-rich liquid was always lower than RMn in the oxide-rich liquid. In order to understand the liquid separation and the distribution of Mn in the two liquid phases, a thermodynamic modeling of this liquid oxysulfide was performed by taking into account strong chemical Short-Range Ordering (SRO) in the framework of the Modified Quasichemical Model in the Quadruplet Approximation. Contrary to the general understanding that Mn attracts S stronger than Fe does and it would have resulted higher Mn content in the sulfide-rich liquid, the present experimental results show that Fe is enriched in the sulfide-rich liquid. This implies that Fe attracts S stronger than Mn does in the liquid phase concerned in the present study. Such a behavior is attributed to the fact that Mn is bound by SiO2 through a formation of (Mn-O-Si) Second-Nearest-Neighbor (SNN) pair, thus oxide-rich liquid attracts more Mn while Fe is distributed more to sulfide-rich liquid. A number of points to be considered for the production of low phosphorus FeMn alloy through the two-phase liquid separation are discussed. © 2013 ISIJ.

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Jo, Y., Lee, H. G., & Kang, Y. B. (2013). Thermodynamics of the MnO-FeO-MnS-FeS-SiO2 system at SiO 2 saturation under reducing condition: Immiscibility in the liquid phase. ISIJ International, 53(5), 751–760. https://doi.org/10.2355/isijinternational.53.751

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