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Procedure for the separation of nickel and Cobalt from ammoniacal Solutions and obtaining carbonate salts of nickel

机译:从氨溶液中分离镍和钴并获得镍碳酸盐的方法

摘要

This Invention relates to non-ferrous hydrometallurgy specifically with the treatment of the obtained solution of the Mineral Processing Technology of carbonate laterite by Ammonia process Known As Caron.There is not an efficient procedure for the separation of cobalt from ammoniacal Solutions by carbonate, due to the variety of amino Complex, difficult separation of the solution.The essence of the invention consists of mixed cationic ion exchange resin Purolite S - type 930 the solution obtained from the Caron process AMMONIUM CARBONATE in a Solution volume of 0.1 - 10.0 / resin volume, for a time between 0.15 - 4 hours, the Resin of the liquor is then separated and washed, then the Resin was washed with a solution desorbedora consists of a mixture of AMMONIUM SULFATE between 100 - 500 g / l Sulphuric Acid between 10 - and 90 g / l, a solution desorbedora / resin 0.5-10 Dur Before a time of 0.15 - 4 hours, thus directly with ni / CO ratios are larger than 500. The solution of Ammonium sulphate and Sulphuric Acid remnant can be recirculated back into the process of Desorption after adjustment of the concentrations of AMMONIUM SULFATE and sulfuric acid. The total Recovery of nickel from the Resin is 89.0 - 99.0%.
机译:本发明涉及有色湿法冶金,特别是涉及通过称为Caron的氨法对碳酸盐红土的矿物加工技术的所得溶液的处理。由于以下原因,没有有效的方法通过碳酸盐从氨溶液中分离钴。本发明的实质由混合阳离子离子交换树脂Purolite S-930组成,该溶液是通过Caron工艺碳酸铵制备的溶液,溶液体积为0.1-10.0 //树脂体积,在0.15-4小时之间的时间里,将液体的树脂分离并洗涤,然后用脱附的溶液洗涤树脂,该溶液由100-500 g / l的硫酸铵混合物在10-500之间的硫酸铵混合物组成和90克/升,解吸附的树脂溶液0.5-10 Dur在0.15-4小时之前,因此直接与ni // CO的比值大于500。调整硫酸铵和硫酸的浓度后,可以将硫酸and和硫酸残渣再循环回解吸过程。从树脂中回收的镍总量为89.0-99.0%。

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