Thermodynamic modeling of nickel and iron reduction from multicomponent silicate melt in bubbling process. Report 2. Reducing agent – a mixture OF Н2 – Н2О

Q3 Materials Science
A. Vusikhis, L. Leont’ev, D. Z. Kudinov, E. Selivanov
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引用次数: 1

Abstract

A number of technologies in ferrous and non-ferrous metallurgy  are based on bubbling processes. For prediction of melting parameters  including the reduction of metals from oxide melt by a reducing gas  in a bubbling layer in industrial aggregates, a thermodynamic modeling technique is proposed based on calculation of the equilibrium in  oxide-melt-metal-gas system. Originality of the technique is that equilibrium is determined for each unit dose of gas introduced into the  working body, with the contents of oxides of metals being reduced in  each subsequent design cycle equal to the equilibrium in the previous  one. For the analysis NiO (1.8  %) – FeO (17.4  %) – CaO (13.5  %)  –  MgO  (1.9  %) – SiO2 (58.0  %) – Al2O3 (7.4  %) oxide system was  taken, closely corresponding to composition of oxidized nickel ore.  The ratio of Н2О/Н2 in gas mixture varies between 0 and 1.0. (1823  K),  amount and composition of formed metal (ferronickel), as well as the  indices (the ratio of slag and metal, the degree of reduction of metals)  are important in implementation of the process under commodity conditions. The increase in hydrogen consumption monotonously reduces  the content of nickel oxide in the melt, while the content of iron oxide  initially increases, and then decreases.  When H2 is introduced in an  amount of about 50 m3 per ton of the melt, the content of nickel oxide  in it is reduced to 0.017  %, and of iron oxide to 16.7  %. Resulting ferronickel contains 61  % Ni, ratio of slag and metal – 42  units. Further  increase in H2 consumption leads to preferential iron reduction. An increase in H2O/H2 ratio worsens the results of reduction of metals from  the melt: decrease in degree of reduction of nickel and iron, increase  in nickel content in the alloy, and the ratio of slag and metal. However,  even with a H2 / H2O ratio of 1.0, which corresponds to 50  % of H2O  in the gas mixture, reduction process does not stop. For comparison,  the work presents data on change in content of nickel and iron oxides,  when metals are restored from similar melts with carbon monoxide.  At a nickel recovery rate of 98  %, indicators are close in case of using  both H2 and CO. However, to achieve them, it is required 2.5  times less hydrogen, and 1.36 times less mixture in which H2O/H2  =  0.11  (H2  –  90  %) than carbon monoxide.
多组分硅酸盐熔体鼓泡还原镍铁的热力学模拟。报告2。还原剂- Н2 - Н2О的混合物
在黑色金属和有色金属冶金中,许多技术都是以鼓泡法为基础的。为了预测工业集料鼓泡层中氧化物熔体中金属的还原性,提出了一种基于氧化物-熔体-金属-气体系统平衡计算的热力学建模技术。该技术的创新之处在于,对每一单位剂量的气体引入工作体,都确定了平衡,在随后的每一个设计周期中,金属氧化物的含量都与前一个设计周期的平衡量相等,分析采用NiO (1.8%) - FeO (17.4%) - CaO (13.5%) - MgO (1.9%) - SiO2 (58.0%) - Al2O3(7.4%)氧化物体系,与氧化镍矿的组成密切相关。混合气体中Н2О/Н2的比值在0 ~ 1.0 (1823 K)之间变化,形成的金属(镍铁)的数量和组成,以及指标(渣与金属的比例,金属的还原程度)对于在商品条件下实施该工艺很重要。随着耗氢量的增加,熔体中氧化镍含量单调降低,而氧化铁含量先升高后降低。当每吨熔体加入50 m3左右的H2时,其氧化镍含量降至0.017%,氧化铁含量降至16.7%,镍铁含镍61%,渣金比为- 42单位。H2用量的进一步增加导致铁的优先还原。H2O/H2比的增大使熔体中金属的还原效果恶化:镍和铁的还原程度降低,合金中镍的含量增加,渣金比增大。然而,即使H2 / H2O比为1.0,即气体混合物中H2O含量为50%,还原过程也不会停止。为了进行比较,这项工作提供了镍和铁氧化物含量变化的数据,当金属从与一氧化碳相似的熔体中恢复时。在镍回收率为98%的情况下,同时使用H2和CO的指标接近,但要达到这一目标,所需的氢气比一氧化碳少2.5倍,H2O/H2 = 0.11 (H2 - 90%)的混合物比一氧化碳少1.36倍。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
Izvestiya Vysshikh Uchebnykh Zavedenij. Chernaya Metallurgiya
Izvestiya Vysshikh Uchebnykh Zavedenij. Chernaya Metallurgiya Materials Science-Materials Science (miscellaneous)
CiteScore
0.90
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