The Use of Liquid Extraction for the Purification of Solutions from the Nickel Production of JSC Kola MMC from Impurities

IF 0.6 4区 材料科学 Q4 METALLURGY & METALLURGICAL ENGINEERING
L. V. Dyakova, A. G. Kasikov, M. V. Jeleznova
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引用次数: 0

Abstract

Studies of the extraction of impurities of calcium(II), magnesium(II), boron(III), and chloride ions from sulfate-chloride nickel solutions have been carried out. As extractants, we used di-2-ethylhexylphosphoric acid (D2EHPA), di-(2,4,4-trimethylpentyl) phosphinic acid (Cyanex 272), trialkylamine (TAA), tributyl phosphate (TBP), and aliphatic alcohols: octanol-1, 2-ethylhexanol, and a by-product of its production—distillation residue (TPRD). According to the results of research, it was established that a mixture of 40% TAA in 2-octanone and TPRD exhibits a high extraction ability with respect to boron(III); the degree of boron extraction is 60.7 and 74.5%, respectively. The effect of the acidity of the aqueous phase and the composition of organic mixtures on the extraction ability of organophosphorus acids D2EHPA and Cyanex272 in the extraction of calcium(II) and magnesium(II) was studied. The optimal concentration of individual extractants was found to be 20 vol % in Escaid 100 solvent and the composition of the mixture (vol %) 15 (D2EHPA) + 5 (Cyanex 272). Individual D2EHPA predominantly extracts calcium(II): extraction of 62% Ca(II) and 15% Mg(II). When using Cyanex272, the extraction of magnesium(II) predominates: extraction of 59% Mg(II) and 20% Ca(II). It is shown that the extraction mixture has higher performance than individual extractants for the extraction of Ca(II) and Mg(II) from nickel solutions in the range of pH 3.0–3.5, at which the coextraction of nickel(II) is negligible. With increasing pH values, the extraction of Ca(II) decreases owing to the increasing extraction of nickel and the displacement of calcium by it from the organic phase. The results of the extraction purification of the nickel electrolyte of JSC Kola MMC with an extraction mixture in the Ni form to exclude pH adjustment at each stage of the process are presented. The experimental data obtained make it possible to conclude that the extraction purification of nickel electrolytes of JSC Kola MMC is promising, as a result of which pure solutions of nickel sulfate with a residual content of ≤0.010 g/dm3 B(III), Ca(II), Mg(II), and chloride ions were obtained.

Abstract Image

用液体萃取法提纯JSC Kola MMC镍生产液中的杂质
对从硫酸盐-氯化镍溶液中提取钙(II)、镁(II)、硼(III)和氯离子杂质进行了研究。作为萃取剂,我们使用了二-2-乙基己基磷酸(D2EHPA)、二-(2,4,4-三甲基戊基)膦酸(Cyanex 272)、三烷基胺(TAA)、磷酸三丁酯(TBP)和脂肪醇:辛醇- 1,2 -乙基己醇及其生产蒸馏残渣(TPRD)的副产物。研究结果表明,在2-辛酮中加入40% TAA和TPRD的混合物,对硼(III)具有较高的萃取能力;硼的萃取度分别为60.7%和74.5%。在钙(II)和镁(II)萃取过程中,研究了水相酸度和有机混合物组成对有机磷酸D2EHPA和Cyanex272萃取能力的影响。在Escaid 100溶剂中,各萃取剂的最佳浓度为20 vol %,混合物(vol %)为15 (D2EHPA) + 5 (Cyanex 272)。单个D2EHPA主要提取钙(II):提取62%的Ca(II)和15%的Mg(II)。当使用Cyanex272时,镁(II)的提取率占主导地位:Mg(II)的提取率为59%,Ca(II)的提取率为20%。结果表明,在pH 3.0 ~ 3.5范围内,混合萃取剂对镍溶液中Ca(II)和Mg(II)的萃取效果优于单一萃取剂,在此范围内,镍(II)的共萃取可以忽略不计。随着pH值的增加,Ca(II)的萃取量减少,原因是镍的萃取量增加,钙被镍从有机相中置换。本文介绍了用Ni形式的萃取液对JSC Kola MMC的镍电解液进行萃取纯化的结果,以排除各阶段的pH调整。实验数据表明,JSC Kola MMC镍电解液的萃取纯化是有前景的,可以得到残留含量≤0.010 g/dm3的纯硫酸镍溶液,其中B(III)、Ca(II)、Mg(II)和氯离子。
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来源期刊
Russian Journal of Non-Ferrous Metals
Russian Journal of Non-Ferrous Metals METALLURGY & METALLURGICAL ENGINEERING-
CiteScore
1.90
自引率
12.50%
发文量
59
审稿时长
3 months
期刊介绍: Russian Journal of Non-Ferrous Metals is a journal the main goal of which is to achieve new knowledge in the following topics: extraction metallurgy, hydro- and pirometallurgy, casting, plastic deformation, metallography and heat treatment, powder metallurgy and composites, self-propagating high-temperature synthesis, surface engineering and advanced protected coatings, environments, and energy capacity in non-ferrous metallurgy.
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