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Preparation of solutions of nitrate(V), nickel(II) from waste solutions containing nickel sulfate and/or chlorides

机译:从含有硫酸镍和/或氯化镍的废液中制备硝酸盐(V),镍(II)的溶液

摘要

Method of industrial production of purified and concentrated nitrate (V) nickel(II) solution from waste nickel solutions containing sulphates and/or chlorides by solvent extraction, including cationic ion exchange extraction,is characterised by the waste water solution containing nickel from 1 to 10% weights,favourably combining with activated charcoal and then filtered, is extracted with a liquid cationite solution in heavy catalytic converted gasoline, with the ratio of the nickel solution to the cationite solution fluctuating within 0,25 to 2,5, the pH of the emulsion being maintained in the range of 3,5 to 4,5, and the temperature is from 30-to 50-degrees, then the organic and aqueous phases are separated,and from the aqueous phase obtained, nickel is extracted into a solution of higher aliphatic acids, selected from a group comprising: 2-ethylhexyphosphoric acid, 2(2,4,4-trimethylpentyl)phosphonic acid and mono-2-ethylhexyl ester of 2-ethylhexyphosphoric acid, dissolved in heavy odaromatized gasoline, the organic phase is then washed with deionised water to dissolve alkali anions and ions in the aqueous phase and then extracted from the organic phase with a nitric acid solution of 20 to 35%,producing a solution of nickel nitrate with a concentration of approximately 14% and salt impurities of other metals below 0,01%.
机译:通过溶剂萃取,包括阳离子交换法,从含有硫酸盐和/或氯化物的废镍溶液中工业生产纯化和浓缩的硝酸镍(V)镍(II)溶液的方法,其特征在于含有1至10的镍的废水溶液重量%,最好与活性炭结合,然后过滤,用重催化转化汽油中的液态阳离子溶液萃取,镍溶液与阳离子溶液的比例在0.25至2.5之间波动,将乳液保持在3.5至4.5的范围内,温度为30至50度,然后分离有机相和水相,并从获得的水相中将镍提取到选自以下的高级脂肪酸:2-乙基己磷酸,2(2,4,4-三甲基戊基)膦酸和2-乙基己磷酸的单-2-乙基己酯脱脂汽油后,将有机相用去离子水洗涤,以将碱阴离子和离子溶解在水相中,然后用20%至35%的硝酸溶液从有机相中萃取,制得浓度为50%的硝酸镍溶液。约14%,其他金属的盐杂质低于0.01%。

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