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Process for the separation of nickel from solutions containing cobalt and nickel salts

机译:从含钴和镍盐的溶液中分离镍的方法

摘要

Nickel is separated from an aqueous solution containing a mixture of cobalt and nickel salts by first precipitating the nickel by adding a metal more electronegative than nickel, for example iron, and also one or more metalloidic compounds formed between sulphur, selenium or tellurium on the one hand, and antimony or arsenic on the other. The separated nickel is then redissolved and the metalloidic compounds regenerated for further use. Copper may also be added in the first stage of the PICT:0853323/III/1 process, either as a soluble salt, the amount of copper added being 0.3-2% by weight of the nickel, or as the sulphide, the copper being 10-25% by weight of the nickel. The first stage may be carried out at 50-100 DEG C. and at a pH of approximately 2.5. Suitable metalloidic compounds include arsenic and antimony sulphides, which may be naturally occurring, such as realgars, orpiments, and stibnites and may be employed in an amount 1-2 times by weight of the nickel present in the solution. Between 1 and 5 times the theoretically required amount of metal more electronegative than nickel may be employed, preferably between 1.1 and 1.3 times, and is preferably in a finely divided state. In an example, a solution of nickel and cobalt sulphate or chloride is heated to above 50 DEG C. with agitation, and copper is added, either as a soluble salt or as the sulphide, which may be added with the metalloidic compound. Arsenic trisulphide and iron are then added, preferably simultaneously, and the pH is maintained at about 2.5 by acid addition, for example hydrochloric acid. The suspended solids are then removed and washed. The cobalt-containing mother liquor remaining is practically free of nickel and copper. The solids are then treated to regenerate the arsenic trisulphide, for example by suspending in water and passing in chlorine until the nickel is substantially completely dissolved, removing the residue, acidifying and adding a sulphide, for example iron sulphide or preferably hydrogen sulphide, to precipitate arsenic and copper sulphides. This precipitate may be freed of copper by dissolving the arsenic sulphide in sodium sulphide solution and acidifying to reprecipitate. The filtrate obtained after the arsenic and copper sulphides have been precipitated is treated to eliminate cobalt and iron by oxidising with chlorine and precipitating ferric hydroxide by adding calcium carbonate to a pH of 3.0-3.5, and precipitating cobalt hydroxide, contaminated with a little nickel which may be recycled to the first stage of the process, by the simultaneous action of chlorine and sodium hydroxide as in Specification 795,410. The cobalt-containing mother liquor obtained after removing the suspended solids in the initial stage of the process may be freed from iron by precipitation as the hydroxide as indicated above. The accompanying flow sheets illustrates the process of the invention.
机译:通过首先添加比镍更具负电性的金属(例如铁)以及一种或多种在硫,硒或碲之间形成的准金属化合物将镍从含有钴和镍盐混合物的水溶液中分离出来手,另一方面是锑或砷。然后将分离出的镍重新溶解,并再生准金属化合物以进一步使用。铜也可以在工艺的第一阶段以可溶性盐的形式添加,铜的添加量为镍的0.3-2%(重量),或者以硫化物的形式添加。铜占镍重量的10-25%。第一步可以在50-100℃和约2.5的pH下进行。合适的准金属化合物包括砷和锑的硫化物,它们可以是天然存在的,例如雄黄,雌黄和硬脂酸酯,并且可以以溶液中镍的重量的1-2倍使用。可以使用理论上所需量为镍的负电性大于镍的1至5倍,优选地为1.1至1.3倍,并且优选为细分状态。在一个实例中,将镍和硫酸钴或氯化钴的溶液在搅拌下加热至50℃以上,并以可溶盐或硫化物的形式添加铜,其可与准金属化合物一起添加。然后优选同时添加三硫化砷和铁,并通过添加酸例如盐酸将pH保持在约2.5。然后除去悬浮的固体并洗涤。剩余的含钴母液几乎不含镍和铜。然后例如通过悬浮在水中并通入氯直到镍基本上完全溶解,除去残留物,酸化并添加硫化物例如硫化铁或优选地硫化氢来处理固体以再生三硫化砷,以使其沉淀。砷和硫化铜。通过将硫化砷溶解在硫化钠溶液中并酸化以重新沉淀,可以使该沉淀物不含铜。砷和硫化铜沉淀后获得的滤液通过用氯氧化并加入碳酸钙至pH为3.0-3.5沉淀氢氧化铁,然后沉淀出被少量镍污染的氢氧化钴来除去钴和铁。通过按照规格795,410的氯和氢氧化钠的同时作用,可将其再循环到工艺的第一阶段。如上所述,在该方法的初始阶段除去悬浮固体之后获得的含钴母液可以通过沉淀以氢氧化物的形式从铁中脱除。所附流程图说明了本发明的方法。

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