DETERMINATION OF THE REACTION RATE CONTROLLING RESISTANCE OF GOETHITE IRON ORE REDUCTION USING CO/CO2 GASES FROM WOOD CHARCOAL

J. Ogbezode, O. Ajide, O. Oluwole, O. Ofi
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Abstract

The quest for suitable reductants for the extraction of iron from ores at minimal energy requirements and maximum degree of metallization is attracting growing researchers’ attention. In the present work, an attempt is made to use non-contact charcoal in the reduction of run-off mine goethite ore at heating temperatures above 570oC. The reduction mechanism adopted is in accordance with Levenspiel’s relations for the shrinking core model. The first stage is concerned with the diffusion of gaseous reactant through the film surrounding the particle to the surface of the solid where Goethite hematite is reduced by CO from wood charcoal to magnetite (3Fe2O3 + CO → 2Fe2O3 + CO2). The second stage involves the penetration of a gaseous reactant through the blanket of ash to the surface of the unreacted core where magnetite is reduced to wustite (Fe3O4 + CO → 3FeO + CO2). The final stage is the reaction of the gaseous reactant with solid at the reaction surface, which is described by the stoichiometry equation where the product consists of fluid and solid (FeO + CO → Fe + CO2). This non-contact charcoal reduction approach is adopted to maximize the benefit of using CO/CO2 gases from charcoal for reduction without the need for beneficiation and concentration. The rate-controlling steps for the reduction kinetics of average particle size 5, 10, 15, and 20 mm at 570, 700, 800, 900, and 1000oC are studied after heat treatment of the ore-wood charcoal in activated carbon reactor at total reduction time of 40 minutes based on literature. Scanning Electron Microscopy (SEM) and Energy Dispersive X-ray (EDX) analysis are done to investigate the spectrometric phase change and metallic components of the ore sample after reduction, respectively. The average percentage metallic iron content of 56.6, 60.8, and 61.7% and degree of metallization of 91.62, 75.96, and 93.6% are achieved from the SEM/EDX analysis of the reduced ore sample at reduction temperature of 570, 800 and 1000oC, respectively. The sharp drop in the degree of metallization of the reduced ore samples is observed at intermediate temperatures 700, 800, 900oC of the reduction. This indicates the tendency of high carbon deposit at the wustite stage of the reduction process at the least temperature and residence time of 5700C and 10 minutes, respectively. This study demonstrates that diffusion through the ash layer is the controlling resistance of the overall reduction process.
木炭co / co2气体还原针铁矿阻力控制反应速率的测定
寻找合适的还原剂,以最小的能量需求和最大程度的金属化从矿石中提取铁,吸引了越来越多的研究人员的关注。在本工作中,尝试在加热温度高于570℃的条件下,使用非接触式木炭还原径流矿针铁矿矿石。所采用的缩减机制符合缩核模型的Levenspiel关系。第一个阶段是气态反应物通过颗粒周围的膜扩散到固体表面,在固体表面,针铁矿赤铁矿被木炭中的CO还原成磁铁矿(3Fe2O3 + CO→2Fe2O3 + CO2)。第二阶段是气态反应物穿过灰层渗透到未反应的核心表面,在那里磁铁矿被还原成浮士体(Fe3O4 + CO→3FeO + CO2)。最后一个阶段是气态反应物与固体在反应表面的反应,用化学计量方程描述,产物由流体和固体组成(FeO + CO→Fe + CO2)。采用这种非接触式木炭还原方法可以最大限度地利用木炭中的CO/CO2气体进行还原,而无需进行选矿和浓缩。在文献资料的基础上,研究了矿木炭在570、700、800、900和1000℃下,总还原时间为40分钟后,在活性炭反应器中热处理后平均粒径为5、10、15和20 mm的还原动力学的速率控制步骤。通过扫描电镜(SEM)和能量色散x射线(EDX)分析,分别研究了还原后矿石样品的光谱相变和金属成分。还原温度为570℃、800℃和1000℃时,还原矿样的平均金属铁含量分别为56.6、60.8和61.7%,金属化程度分别为91.62、75.96和93.6%。在还原温度为700、800、900℃时,还原矿样的金属化程度急剧下降。这表明在还原过程中,在最低温度5700C和停留时间10min时,浮士体阶段有高碳沉积的趋势。研究表明,通过灰层的扩散是整个还原过程的控制阻力。
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