Mechanism and Kinetics of Scandium Extraction from High-Pressure Leachate of Iron-Aluminum Residue

IF 2.3 4区 材料科学 Q3 MATERIALS SCIENCE, MULTIDISCIPLINARY
JOM Pub Date : 2026-09-15 DOI:10.1007/s11837-026-08616-8
Yunpeng Du, Chunmin Zhang, Yihui Chen, Jingning Yang, Wenwei Wu
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引用次数: 0

Abstract

Laterite nickel ore, a crucial resource for nickel production, contains associated rare earth scandium (Sc) at 50–80 g/ton, which is difficult to extract directly from the raw ore. Currently, the high-pressure acid leaching (HPAL) process for laterite nickel ore is becoming mainstream; during this primary HPAL step, Sc remains in the solid residue because the leaching conditions are optimized for Ni and Co recovery. The Sc-bearing iron‑aluminum residue is then subjected to a second HPAL step with higher acidity and temperature, which effectively dissolves Sc. However, this second HPAL step dissolved not only Sc but also Fe and Al, necessitating selective Sc extraction from the leachate. This study systematically investigated the extraction efficiency of Sc using a binary system of bis(2,4,4-trimethylpentyl)phosphinic acid (Cyanex 272) and di(2-ethylhexyl) (2-ethylhexyl) phosphonate (Cextrant 230), employing leachate generated from prior experiments. At a Cyanex 272 molar fraction of 0.6 (total extractant concentration 0.1 mol/L, room temperature, aqueous-to-organic phase ratio 1:1), the system exhibited optimal synergistic extraction for Sc, achieving separation coefficients of 2.89 and 2.35 for Fe and Al, respectively. Based on these findings, the chemical formula of the final extracted complex was determined via the slope analysis method. Furthermore, the kinetics and mass transfer processes of the extraction reaction were systematically studied using the constant interfacial cell technique. The extraction of Sc3+ by the Cyanex 272-Cextrant 230 system was identified as a first-order reaction. The forward extraction rate was found to be governed by a mixed diffusion-and-chemical-reaction mechanism, with the reaction occurring at the organic-aqueous interface. A rate equation was derived based on the extraction mechanism calculations. This research provides valuable insights for Sc recovery from laterite nickel ore.

铁铝渣高压渗滤液中钪的萃取机理及动力学研究
红土镍矿是镍生产的重要资源,伴生稀土钪(Sc)含量为50 ~ 80 g/t,难以直接从原矿中提取,目前红土镍矿采用高压酸浸(HPAL)工艺正成为主流;在初级HPAL步骤中,由于浸出条件对镍和钴的回收进行了优化,Sc仍留在固体残渣中。含钪的铁铝渣进行第二步HPAL处理,在更高的酸度和温度下,有效地溶解了Sc。然而,第二步HPAL处理不仅溶解了Sc,还溶解了Fe和Al,因此需要从渗滤液中选择性地提取Sc。本研究系统考察了二(2,4,4-三甲基戊基)膦酸(Cyanex 272)和二(2-乙基己基)(2-乙基己基)膦酸盐(萃取剂230)二元体系对Sc的萃取效率。当萃取剂总浓度为0.1 mol/L,室温,水有机比为1:1时,该体系对Sc的协同萃取效果最佳,Fe和Al的分离系数分别为2.89和2.35。在此基础上,通过斜率分析法确定了最终萃取物的化学式。采用恒界面池技术对萃取反应的动力学和传质过程进行了系统的研究。cyanex272 - cextrant 230体系对Sc3+的萃取为一级反应。正向萃取速率受扩散-化学混合反应机制控制,反应发生在有机-水界面。在萃取机理计算的基础上,推导了萃取速率方程。该研究为从红土镍矿石中回收钪提供了有价值的见解。
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来源期刊
JOM
JOM 工程技术-材料科学:综合
CiteScore
4.50
自引率
3.80%
发文量
540
审稿时长
2.8 months
期刊介绍: JOM is a technical journal devoted to exploring the many aspects of materials science and engineering. JOM reports scholarly work that explores the state-of-the-art processing, fabrication, design, and application of metals, ceramics, plastics, composites, and other materials. In pursuing this goal, JOM strives to balance the interests of the laboratory and the marketplace by reporting academic, industrial, and government-sponsored work from around the world.
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