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Some Observations on the Chloride Based Treatment of Nickel-Copper-Cobalt Mattes

机译:基于氯化物处理镍-铜-钴哑光的一些观察

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Smelting of nickel sulphide concentrates produces a liquid Fe/Ni/Cu/Co/PGM sulphide, also called furnace matte, from which nearly all of the iron and most of the sulphur are removed by air oxidation at approximately 1200℃, in a process called converting. The sulphur is emitted from the converter as SO_2. The final product is called finished or converter matte, or simply "matte", and is cooled slowly, or fast by water granulation, depending on subsequent processing. The smelting route is still the most elegant and economical method to remove the iron and gangue impurities as a disposable slag from such concentrates on a large scale. It is practised in smelters worldwide. Producing saleable nickel, cobalt, copper and PGM's (Platinum Group Metals) from these mattes has been achieved by a variety of methods, mainly hydrometallurgical. Refining processes based on sulphate chemistry were the logical first choice, followed by carbonyl, ammoniacal and chloride based processes. This paper specifically compares sulphate and chloride systems. Chloride based refining was pioneered successfully by Falconbridge at its Nikkelverk, Kristiansand-S, Norway refinery and has been adopted at refineries in France and Japan. The advantages of treating matte by the chloride route for past and future producers are discussed in the paper, with particular emphasis on the low cost of cobalt recovery, if solvent extraction can be applied. The latter depends on creating a nickel chloride leach liquor with a high chloride normality, which dictates the lixiviant to be either super-azeotropic HC1 or chlorine gas. Process recovery of the lixiviant from the solubilised nickel chloride is imperative for environmental and cost reasons. Problems and opportunities with applicable recovery systems for HCl and Cl_2 will also be addressed in detail. Finally, some speculation is presented as to how recent chloride technology developments could be used to advantage in chloride based processing of mattes.
机译:冶炼硫化镍精矿会产生液态Fe / Ni / Cu / Co / PGM硫化物,也称为炉磨砂,在大约1200℃的温度下,通过空气氧化,几乎所有的铁和大部分的硫都被空气氧化除去。转换。硫从转炉中以SO_2的形式排出。最终产品称为成品或转炉哑光产品,或简称为“哑光”产品,视后续加工而定,通过水造粒缓慢或快速冷却。熔炼路线仍然是从此类精矿中大规模去除铁和煤gang石杂质(即一次性炉渣)的最优雅,最经济的方法。它在全世界的冶炼厂中都有实践。从这些消光粉生产可销售的镍,钴,铜和PGM(铂族金属)已通过多种方法实现,主要是湿法冶金。合理的选择是基于硫酸盐化学的精炼工艺,其次是基于羰基,氨和氯化物的工艺。本文专门比较了硫酸盐和氯化物系统。 Falconbridge在挪威的Kristiansand-S的Nikkelverk的炼油厂成功地率先进行了基于氯化物的炼油,并已在法国和日本的炼油厂采用。本文讨论了通过氯化物途径为过去和将来的生产商处理哑光的优势,特别强调了如果可以使用溶剂萃取的话,钴回收的低成本。后者取决于产生具有高氯化物正态性的氯化镍浸出液,这表明浸滤剂是超共沸HCl或氯气。由于环境和成本的原因,必须从溶解的氯化镍中回收浸滤剂。适用的HCl和Cl_2回收系统的问题和机遇也将得到详细解决。最后,对于如何利用最新的氯化物技术在基于氯化物的哑光加工中发挥优势提出了一些推测。

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