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Low-lead nickel production by electrowinning of lead contaminated nickel chloride solution in a membrane equipped electrolytic cell

机译:通过在膜的电解细胞中的铅污染镍氯化镍溶液的电氢化通过电滤网的低引出镍生产

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Lead removal has been problematic in nickel production by electrowinning from chloride solutions, as developed by Falconbridge. The Cl{sub}2 leach liquor needs to be diluted by electrolyte to allow precipitation of the lead prior toelectrowinning. This results in higher solution purification costs and an aversion to consider lead contaminated (secondary) feeds.In this paper, the electrowinning of nickel chloride is carried out in a membrane equipped electrolytic cell. When lead containing nickel solutions are fed into the anode compartment and the anolyte is separated from the catholyte with a cation exchangemembrane, lead remains in the anolyte due to the presence of a negatively charged chloride complex. The positive nickel ions migrate preferentially through the membrane to the catholyte, allowing a lower lead nickel cathode to be produced. Leadconcentration in the catholyte and the cathode product has been tested as a function of lead concentration in the anolyte. Results are presented and discussed.
机译:通过Falconbridge开发的从氯化物溶液中电氢化,铅去除在镍生产中存在问题。需要通过电解质稀释Cl {sub} 2浸出液以允许在宁到电量之前沉淀铅。这导致较高的溶液净化成本和厌恶以考虑铅污染的(二次)饲料。在本文中,氯化镍的电解在配备的电解槽中进行。当含有镍溶液的铅溶液进料到阳极室中时,通过用阳离子交换膜与阴极电解液分离出阳极电解液,由于存在带负电荷的氯化物络合物,铅保留在阳极物中。正镍离子优选地通过膜迁移到阴极电解液,允许制备下引线镍阴极。在阴极电解液和阴极产品中的脱气浓缩已被测试为阳极电解液中的铅浓度的函数。提出和讨论了结果。

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