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Naji, M. |
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Motta, Antonella |
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Aletan, Dirar |
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Mohamed, Tarek |
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Ertürk, Emre |
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Taccardi, Nicola |
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Kononenko, Denys |
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Petrov, R. H. | Madrid |
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Alshaaer, Mazen | Brussels |
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Bih, L. |
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Casati, R. |
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Muller, Hermance |
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Kočí, Jan | Prague |
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Šuljagić, Marija |
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Kalteremidou, Kalliopi-Artemi | Brussels |
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Azam, Siraj |
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Ospanova, Alyiya |
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Blanpain, Bart |
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Ali, M. A. |
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Popa, V. |
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Rančić, M. |
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Ollier, Nadège |
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Azevedo, Nuno Monteiro |
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Landes, Michael |
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Rignanese, Gian-Marco |
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Wimmer, Gerald
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Publications (5/5 displayed)
- 2023The Behavior of Phosphorus in the Hydrogen-Based Direct Reduction—Smelter Ironmaking Routecitations
- 2023The Behavior of Direct Reduced Iron in the Electric Arc Furnace Hotspotcitations
- 2022Investigations on the Interaction Behavior between Direct Reduced Iron and Various Meltscitations
- 2019Kinetics and Mechanisms of Dolime Dissolution in Steelmaking Slagcitations
- 2017Influence of Magnesium Oxide content on kinetics of lime dissolution in steelmaking slagscitations
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article
Influence of Magnesium Oxide content on kinetics of lime dissolution in steelmaking slags
Abstract
The kinetics of lime dissolution containing different amounts of magnesium oxide (4.3–7.6%) in steelmaking slags has been studied in a non-stationary diffusion, at temperatures ranging from 1 300–1 600°C,<br/>directly in the hot process. The decrease in solubility of lime with the increasing content of magnesium<br/>oxide is due to the formation of high temperature solid chemical compounds (Ca2SiO4, (Mg,Fe)2SiO4) and<br/>solutions based on MgO like ((Mg,Fe) O) in the volume of lime samples. Formed slightly soluble phases<br/>hinder the process of CaO dissolution and slow down the rate of dissolution of lime samples. Based on<br/>differential equations of mass balance of the dissolving substance and taking into account its transition<br/>into the melt phase, and accumulation in the consistently dissolving layers of solid, values of mass transfer coefficients and diffusion coefficients were calculated. Mass transfer coefficients, despite a decrease<br/>in the concentration gradient, increase in the process of slag saturation with lime. Activation energy has<br/>been calculated under conditions of non-stationary linear and spatial semi-infinite diffusion. Based on the<br/>dependency of the logarithm of diffusion coefficients on the inverse temperature derived value of the<br/>activation energy of diffusion is 230.2±14.0 kJ/mol.