李刚, 丁成义, 宣森炜, 吕学伟, 吴珊珊. 铁酸钙与赤铁矿非等温还原动力学[J]. 工程科学学报, 2018, 40(11): 1317-1324. DOI: 10.13374/j.issn2095-9389.2018.11.005
引用本文: 李刚, 丁成义, 宣森炜, 吕学伟, 吴珊珊. 铁酸钙与赤铁矿非等温还原动力学[J]. 工程科学学报, 2018, 40(11): 1317-1324. DOI: 10.13374/j.issn2095-9389.2018.11.005
LI Gang, DING Cheng-yi, XUAN Sen-wei, LÜ Xue-wei, WU Shan-shan. Non-isothermal reduction kinetics of calcium ferrite and hematite[J]. Chinese Journal of Engineering, 2018, 40(11): 1317-1324. DOI: 10.13374/j.issn2095-9389.2018.11.005
Citation: LI Gang, DING Cheng-yi, XUAN Sen-wei, LÜ Xue-wei, WU Shan-shan. Non-isothermal reduction kinetics of calcium ferrite and hematite[J]. Chinese Journal of Engineering, 2018, 40(11): 1317-1324. DOI: 10.13374/j.issn2095-9389.2018.11.005

铁酸钙与赤铁矿非等温还原动力学

Non-isothermal reduction kinetics of calcium ferrite and hematite

  • 摘要: 采用非等温热重的方法,在30% CO+70% N2(体积分数)气氛下,以10 K·min-1升温至1123 K的过程中,比较了铁酸钙与赤铁矿的逐级还原过程及其还原动力学.结果表明:铁酸钙和赤铁矿开始还原温度分别为873 K和623 K;由反应速率与反应度的关系及分阶段X射线衍射物相分析发现,铁酸钙还原过程为两段式反应(CaO·Fe2O3→2CaO·Fe2O3→Fe),而赤铁矿还原过程为传统的三段式反应(Fe2O3→Fe3O4→FeO→Fe).通过Freeman-Carroll法计算得知铁酸钙和赤铁矿的还原平均活化能分别为49.88和43.74 kJ·mol-1;铁酸钙还原过程符合随机成核随后生长模型,动力学模式函数为Avrami-Erofeev方程,其积分形式为-ln (1-α)n;而赤铁矿还原过程动力学机理分为两部分,在还原度α为0.1~0.5时,为三级化学反应模型,模式函数积分形式为1-(1-α)3;在α为0.5~0.9时,符合二维圆柱形扩散模型,动力学模式函数为Valensi方程,其积分形式为α+(1-α)ln (1-α).

     

    Abstract: The reduction behaviors of sinter and lump ores, which account for 90% of the raw materials charged into blast furnace process, are important to coke reduction in the ironmaking industry. The isothermal reduction behaviors of sinter and lump ores have been extensively studied; however, non-isothermal conditions, which are more consistent with the temperature change characteristics in a blast furnace, have been rarely investigated in terms of their reduction processes. Studies on the reduction behaviors of calcium ferrite and hematite, which are individually contained in sinter and lump ores, can provide more significant guidance to the practical operation. Comparisons of the reduction behaviors of calcium ferrite and hematite involves thermodynamic parameters such as the starting reduction temperature and kinetic parameters such as activation energy and model function. Considering reduction processes, hematite has been clearly explored by numerous works to an extent far more than calcium ferrite. In addition, in studying the reduction behaviors of calcium ferrite and hematite, pellet samples of 1-100 mm were the focus in the past and rarely micron-sized powder samples (1-100 μm). However, nowadays, micron-sized particles are extensively applied on iron ores reduction in fluidized bed process and non-blast furnace process, such as FINEX® method; therefore, in this study, calcium ferrite and hematite were compared, considering their reduction routes and reduction kinetics. Non-isothermal reduction experiments of powdery calcium ferrite and hematite heated up to 1123 K with a rate of 10 K·min-1 in a continuous stream of 30% CO and 70% N2 were conducted through thermo-gravimetric analysis. The results show that the reduction processes of calcium ferrite and hematite begin at 873 K and 623 K, respectively. Reduction rate analysis and subsequent X-Ray diffraction measurements at various stages reveal that the reduction of calcium ferrite can be divided into two steps:CaO·Fe2O3 → 2CaO·Fe2O3 → Fe, whereas that of hematite mainly comprises three steps:Fe2O3 → Fe3O4 →FeO → Fe. The activation energy was calculated by Freeman-Carroll method, and the average values of calcium ferrite and hematite reduction are 49.88 and 43.74 kJ·mol-1, respectively. The reduction of calcium ferrite can be described by random instant nucleation and two-dimensional growth of nuclei model; its corresponding model function is Avrami-Erofeev equation with an integral form of-ln(1-α)n, whereas the reduction of hematite was initially expressed by a tertiary chemical reaction model (reduction degree α=0.1~0.5) with an integral form of 1-(1-α)3, and subsequently by a two-dimensional cylindrical diffusion model (α=0.5~0.9) with an integral form of α+(1-α) ln(1-α).

     

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