Choi Kyoung Hun, Azimi Gisele
Laboratory for Strategic Materials, Department of Chemical Engineering and Applied Chemistry, University of Toronto 200 College Street Toronto ON M5S 3E5 Canada.
Department of Materials Science and Engineering, University of Toronto 184 College Street Toronto Ontario M5S 3E4 Canada
RSC Adv. 2023 Sep 27;13(41):28501-28512. doi: 10.1039/d3ra04280d. eCollection 2023 Sep 26.
NiSO·6HO is an important salt for the battery-making industry. The extraction of nickel sulfate relies on the hydrometallurgical processing of nickel ores as well as the recycling of nickel-containing products. The last step in hydrometallurgical processing is the crystallization of nickel sulfate. Because of the similar ionic radius and ionic charge between nickel and magnesium ions, magnesium undergoes isomorphous substitution and replaces nickel ions in the crystal lattice structure of NiSO·6HO. This poses a challenge as achieving the desired metal salt purity is difficult, resulting in an inferior cathode material for nickel-containing batteries. In this work, the removal of magnesium during the purification process of NiSO·6HO crystals a repulping process was thoroughly investigated. Moreover, the impurity uptake mechanisms of magnesium into NiSO·6HO crystals were investigated. The results indicated that repulping NiSO·6HO crystals with a saturated NiSO solution results in 77% removal of magnesium. Using a second-stage repulping process is less effective with only 26% magnesium removal. The purification efficiency of the two repulping stages was quantified by the equilibrium distribution coefficient, which corroborates the trend of decreased removal of magnesium in the second stage of repulping compared with the first stage. The primary impurity uptake mechanisms of magnesium into NiSO·6HO crystals were identified to be surface adsorption and lattice substitution (isomorphous substitution).
六水合硫酸镍(NiSO₄·6H₂O)是电池制造行业的一种重要盐类。硫酸镍的提取依赖于镍矿石的湿法冶金加工以及含镍产品的回收利用。湿法冶金加工的最后一步是硫酸镍的结晶。由于镍离子和镁离子的离子半径和离子电荷相似,镁会发生同晶替代,取代六水合硫酸镍(NiSO₄·6H₂O)晶格结构中的镍离子。这带来了一个挑战,因为难以达到所需的金属盐纯度,从而导致含镍电池的负极材料质量较差。在这项工作中,对六水合硫酸镍(NiSO₄·6H₂O)晶体提纯过程中镁的去除——一种再浆化过程进行了深入研究。此外,还研究了镁进入六水合硫酸镍(NiSO₄·6H₂O)晶体的杂质吸收机制。结果表明,用饱和硫酸镍溶液对六水合硫酸镍(NiSO₄·6H₂O)晶体进行再浆化可去除77%的镁。采用第二阶段再浆化过程效果较差,仅能去除26%的镁。通过平衡分配系数对两个再浆化阶段的提纯效率进行了量化,这证实了与第一阶段相比,第二阶段再浆化过程中镁去除率下降的趋势。已确定镁进入六水合硫酸镍(NiSO₄·6H₂O)晶体的主要杂质吸收机制为表面吸附和晶格替代(同晶替代)。