富铁镍渣还原金属化球团的熔分实验研究

Experimental study on the melting separation of metallization pellets reduced from iron-rich nickel slag

  • 摘要: 富铁镍渣中铁、镍、钴、铜等有价金属资源的高效回收是解决镍渣资源综合利用的关键技术瓶颈之一。本文以改性镍渣还原金属化球团为研究对象,首先采用FactSage软件对金属化球团CaO-MgO-SiO2渣系进行热力学分析,借助相图和平衡计算明确了二次渣的组成和熔体特性;然后通过实验考察了熔分温度、碱度等因素对金属化球团中铁、镍、钴、铜等有价金属回收率的影响,探究了目标金属在熔分过程的迁移富集特征规律,明确了熔分工艺较优参数,并对改性镍渣金属化球团熔分过程机制进行了分析。热力学计算结果表明:改性镍渣金属化球团的渣系碱度在0.7~0.9范围时,熔化温度低于1 400 ℃,黏度为0.2~0.4 Pa·s,二次渣相为辉石相。实验结果表明:当熔分温度为1 600 ℃、碱度为0.9时,熔分铁的回收率可达95.31%,同时镍、钴、铜等金属的富集回收率均较优。

     

    Abstract: The efficient recovery of valuable metal resources, such as iron, nickel, cobalt and copper, from iron-rich nickel slag represents a key technical bottleneck in the comprehensive utilization of nickel slag resources. This study focused on metallized pellets produced by the reduction of modified nickel slag. Firstly, the thermodynamic analysis of the CaO-MgO-SiO2 slag system for these pellets was carried out using FactSage software, and the composition of secondary slags and melt characteristics were determined through phase diagrams and equilibrium calculations. Then, the effects of melting temperature, alkalinity and other factors on the recovery rates of valuable metals, such as iron, nickel, cobalt and copper in metallized pellets were investigated through experiments. The migration and enrichment characteristics of the target metals were also explored during the melting separation process, the optimal processing parameters were identified, and the underlying mechanism was analyzed. Thermodynamic calculations showed that when the slag system alkalinity of modified nickel slag metallized pellets was within the range of 0.7~0.9, the melting temperature was lower than 1 400 ℃, the viscosity was 0.2~0.4 Pa·s, and the secondary slag phase was the pyroxene phase. Experimental results showed that when the melting temperature was 1 600 ℃, and the alkalinity was 0.9, the recovery ratio of melted iron reached 95.31%. The enrichment and recovery ratios of nickel, cobalt and copper were all satisfactory.

     

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