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Ju Xu, Guojun Ma, Jie Xu, Mengke Liu, Xiang Zhang, Dingli Zheng, and Junlong Li, Kinetics of isothermal reduction of carbon-containing silicomanganese dust, Int. J. Miner. Metall. Mater.,(2025). https://dx.doi.org/10.1007/s12613-024-3064-8
Ju Xu, Guojun Ma, Jie Xu, Mengke Liu, Xiang Zhang, Dingli Zheng, and Junlong Li, Kinetics of isothermal reduction of carbon-containing silicomanganese dust, Int. J. Miner. Metall. Mater.,(2025). https://dx.doi.org/10.1007/s12613-024-3064-8
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含碳硅锰合金冶炼粉尘等温还原动力学研究

摘要: 硅锰粉尘中含有大量Si、Mn等元素,可作为硅锰冶炼的原料。但由于粉尘粒度细小,直接加入矿热炉会影响矿热炉透气性,导致冶炼过程中还原反应不完全。本文将硅锰合金冶炼粉尘、石墨粉以及其他添加剂压制成含碳压块,在不同碳氧(C/O)摩尔比、助熔剂含量和还原温度的条件下,采用等温热失重法研究了粉尘含碳压块的自还原过程。建立了不同温度下粉尘含碳压块的还原动力学模型。结果表明,当压块C/O摩尔比为1.2时,反应分数约为90%,还原效果最佳。添加CaF2会降低粉尘含碳压块的熔点和粘度,增加反应的还原速率。随着还原温度的升高,粉尘含碳压块的还原速率增大。气相扩散控制粉尘含碳压块的还原反应速率。同时,对压块还原过程进行动力学分析,以5 min为界,两个扩散阶段的表观活化能分别为56.10和100.52 kJ/mol。动力学方程表示为1 − (1 − ƒ)1/32 = 0.69·e−56100/RTt和1 − (1 − ƒ)1/32 = 2.06·e−100520/RTt

 

Kinetics of isothermal reduction of carbon-containing silicomanganese dust

Abstract: Silicomanganese dust contains large amounts of valuables, such as Si and Mn, which can be used as raw materials for the smelting of silicomanganese. However, the direct addition of dust to the submerged arc furnace can influence the permeability of burden due to the fine particle size of dust, which results in incomplete reduction reactions during the smelting process. In this paper, silicomanganese dust, graphite powder, and other additives were pressed to form carbon-containing dust briquettes, and the self-reduction process of the dust briquettes was investigated through the isothermal thermogravimetric method with different carbon–oxygen (C/O) molar ratios, contents of fluxing agents, and reduction temperatures. Various reduction kinetic models for dust briquettes at different temperatures were established. The results show that the reaction fraction of the dust briquettes was about 90% at a C/O molar ratio of 1.2 with optimal reduction efficiency. The addition of CaF2 contributed to the decrease in the melting point and viscosity of dust briquettes, which increased their reduction rate. As the reduction temperature increased, the reduction rate of dust briquettes increased. The reduction reaction rate of dust briquettes was controlled through gas-phase diffusion. Meanwhile, their reduction process was analyzed kinetically, with the reaction time of 5 min as the dividing line. The apparent activation energies for the two diffusion stages were 56.10 and 100.52 kJ/mol, respectively. The kinetic equations are expressed as 1 − (1 − ƒ)1/32 = 0.69e−56100/RTt and 1 − (1 − ƒ)1/32 = 2.06e−100520/RTt.

 

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