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Electrowinning of cobalt from chloride solution - A pilot plant study

机译:氯化物溶液中钴的电沉积-中试工厂研究

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An electrowinning pilot plant has been constructed at Falconbridge Nikkelverk A/S, Kristiansand, Norway. The equipment consists of a mixing tank where the electrolyte composition and temperature are controlled, an electrowinning tank equipped with five cathodes and six anodes of commercial size and design and a dechlorination facility. Electrowinning experiments were carried out in this pilot plant using acid cobalt chloride solution from the cobalt tankhouse. Key parameters were varied to obtain an improved understanding of the cobalt electrowinning process, focusing on the detrimental deposition of cobalt oxide on dimensionally stable anodes. The extent of anode scaling was found to be dependent on the electrowinning conditions. Low pH, temperature and cobalt concentration resulted in less scale being formed, however at the expense of cobalt current efficiency and cell voltage, adversely affecting electrowinning production capacity and energy consumption. When operating at high acidity, pH in the anolyte was higher than in the catholyte, which is believed to be due to H~+ ions taking part in the current transport across the diaphragm, migrating out of the bags surrounding each anode.
机译:在挪威克里斯蒂安桑的Falconbridge Nikkelverk A / S处建造了一个电沉积试点工厂。该设备包括一个控制电解液成分和温度的混合槽,一个配有五个具有商业规模和设计的阴极和六个阳极的电解沉积槽以及一个脱氯设备。在该中试工厂中使用来自钴罐的酸性氯化钴溶液进行了电沉积实验。改变关键参数以获得对钴电积过程的更好理解,重点是尺寸稳定的阳极上氧化钴的有害沉积。发现阳极结垢的程度取决于电解沉积条件。低pH值,温度和钴浓度导致形成的水垢较少,但是以钴电流效率和电池电压为代价,不利地影响了电解沉积的生产能力和能耗。当在高酸度下运行时,阳极电解液中的pH值高于阴极电解液中的pH,这被认为是由于H +离子参与了跨膜的电流传输,并从围绕每个阳极的袋子中迁移出来。

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