| Investigation of the kinetic mechanism of the demanganization reaction between carbon-saturated liquid iron and CaF2-CaO-SiO2-based slags |
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| 引用本文： | Sheng-chao Duan,Chuang Li,Han-jie Guo,Jing Guo,Shao-wei Han,Wen-sheng Yang. Investigation of the kinetic mechanism of the demanganization reaction between carbon-saturated liquid iron and CaF2-CaO-SiO2-based slags[J]. 矿物冶金与材料学报, 2018, 25(4): 399-404. DOI: 10.1007/s12613-018-1584-9 |
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| 作者姓名： | Sheng-chao Duan Chuang Li Han-jie Guo Jing Guo Shao-wei Han Wen-sheng Yang |
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| 作者单位： | School of Metallurgical and Ecological Engineering, University of Science and Technology Beijing, Beijing 100083, China; |
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| 基金项目： | The authors are thankful for the support from the Nation-al Natural Science Foundation of China;the Beijing Key Laboratory of Special Melting and Preparation of High-End Metal Materials in the School of Metallurgical and Ecological Engineering of University of Science and Technology Beijing,China |
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| 摘 要： | The demanganization reaction kinetics of carbon-saturated liquid iron with an eight-component slag consisting of CaO-SiO2-MgO-FeO-MnO-Al2O3-TiO2-CaF2 was investigated at 1553, 1623, and 1673 K in this study. The rate-controlling step (RCS) for the demanganization reaction with regard to the hot metal pretreatment conditions was studied via kinetics analysis based on the fundamental equation of heterogeneous reaction kinetics. From the temperature dependence of the mass transfer coefficient of a transition-metal oxide (MnO), the apparent activation energy of the demanganization reaction was estimated to be 189.46 kJ·mol-1 in the current study, which indicated that the mass transfer of MnO in the molten slag controlled the overall rate of the demanganization reaction. The calculated apparent activation energy was slightly lower than the values reported in the literature for mass transfer in a slag phase. This difference was attributed to an increase in the "specific reaction interface" (SRI) value, either as a result of turbulence at the reaction interface or a decrease of the absolute amount of slag phase during sampling, and to the addition of calcium fluoride to the slag.
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| 关 键 词： | demanganization reaction kinetics reaction mechanism kinetic model rate-controlling step mass transfer coefficient apparent activation energy |
Investigation of the kinetic mechanism of the demanganization reaction between carbon-saturated liquid iron and CaF2–CaO–SiO2-based slags |
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| Sheng-chao Duan,Chuang Li,Han-jie Guo,Jing Guo,Shao-wei Han,Wen-sheng Yang. Investigation of the kinetic mechanism of the demanganization reaction between carbon-saturated liquid iron and CaF2–CaO–SiO2-based slags[J]. International Journal of Minerals,Metallurgy and Materials, 2018, 25(4): 399-404. DOI: 10.1007/s12613-018-1584-9 |
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| Authors: | Sheng-chao Duan Chuang Li Han-jie Guo Jing Guo Shao-wei Han Wen-sheng Yang |
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| Affiliation: | 1.School of Metallurgical and Ecological Engineering,University of Science and Technology Beijing,Beijing,China;2.Beijing Key Laboratory of Special Melting and Preparation of High-End Metal Materials,Beijing,China;3.China Metallurgical Planning and Research Institute,Beijing,China |
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| Abstract: | The demanganization reaction kinetics of carbon-saturated liquid iron with an eight-component slag consisting of CaO-SiO2-MgO-FeO-MnO-Al2O3-TiO2-CaF2was investigated at 1553, 1623, and 1673 K in this study. The rate-controlling step (RCS) for the demanganization reaction with regard to the hot metal pretreatment conditions was studied via kinetics analysis based on the funda-mental equation of heterogeneous reaction kinetics. From the temperature dependence of the mass transfer coefficient of a transition-metal oxide (MnO), the apparent activation energy of the demanganization reaction was estimated to be 189.46 kJ·mol-1in the current study, which indicated that the mass transfer of MnO in the molten slag controlled the overall rate of the demanganization reaction. The calculated appar-ent activation energy was slightly lower than the values reported in the literature for mass transfer in a slag phase. This difference was attri-buted to an increase in the "specific reaction interface" (SRI) value, either as a result of turbulence at the reaction interface or a decrease of the absolute amount of slag phase during sampling, and to the addition of calcium fluoride to the slag. |
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