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高碱度电炉粉尘碳热还原动力学及反应机制

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为研究高碱度电炉粉尘碳热还原反应动力学和反应机制.通过不同温度条件下含碳高碱度电炉粉尘的物相(XRD)解析其物相转变过程.采用热重分析法对不同配碳量和碱度的高碱度电炉粉尘进行热重实验,实验结果表明,配碳量和碱度能促进电炉粉尘碳热还原反应,提高碱度能降低反应所需的温度.最后,通过非等温动力学分析法对高碱度电炉粉尘进行动力学分析,基于KAS法和Coats-Redfern法,确定了主要的动力学参数,根据转化率(α)高碱度电炉粉尘碳热还原过程分为3个阶段:α=0~0.082,α=0.082~0.5和α=0.5~1.0.第1阶段,平均活化能为380.68kJ/mol,反应由一维扩散控制.第2阶段和第3阶段的平均活化能分别为318.79 kJ/mol和264.42kJ/mol,其反应均由化学反应控制.
Kinetics and reduction mechanism of high-basicity electric arc furnace dust by carbothermal reduction
In order to investigate the kinetics and reduction mechanism of carbothermal reduction reaction of high-basicity electric arc furnace dust(EAFD),the phase transition process of carbon containing high-basicity EAFD via XRD under different temperatures was analyzed.The high-basicity EAFD with different carbon contents and basicities were analyzed by the thermogravimetric analysis method.The results show that the carbon content and basicity can promote the carbothermal reduction reaction of EAFD,and increasing basicity can reduce the temperature required for the reaction.Finally,the kinetics of high-basicity EAFD was analyzed by a non-isothermal kinetic analysis method.Based on the KAS method and Coats-Redfern methods,the kinetic parameters and mechanism function were determined.The carbothermal reduction process of high-basicity EAFD was divided into three stages on the basis of the conversion rate(α):α=0-0.082,α=0.082-0.5,and α=0.5-1.0.The average activation energy of the first stage was 380.68 kJ/mol,and the reaction mechanism was one-dimensional diffusion.The average activation energy was 318.79 kJ/mol for the second stage and 264.42 kJ/mol for the third stage.The chemical reaction function was discovered as the most suitable mechanism in the second and third stage.

electric arc furnace dustcarbothermal reductionbasicitynon-isothermal kinetics

余水、毛瑞、王飞、姚海威

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江苏省(沙钢)钢铁研究院环保资源研究室,江苏张家港 215625

电炉粉尘 碳热还原 碱度 非等温动力学

2024

钢铁研究学报
中国钢研科技集团有限公司

钢铁研究学报

CSTPCD北大核心
影响因子:0.997
ISSN:1001-0963
年,卷(期):2024.36(2)
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