首页> 外文会议>Proceedings of the Nickel-Cobalt 97 International Symposium August 17-20, 1997, Sudbury, Ontario, Canada >The acid pressure leach process for nickel and cobalt laterite. Part II: Review of operations at Fort Saskatchewan
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The acid pressure leach process for nickel and cobalt laterite. Part II: Review of operations at Fort Saskatchewan

机译:镍和红土钴酸的酸浸法。第二部分:萨斯喀彻温堡行动回顾

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The nickel-cobalt sulphides produced from limonitic laterite ores by Moa Nickel S.A. in Cuba are shipped to the Corefco nickel-cobalt refinery in Canada. This refinery is the former Sherritt Gordon nickel refinery in Fort Saskatchewan, Alberta, which has been in operation since 1954. Major changes to the refining process were required to handle the Moa sulphide feed with its unusually high cobalt content. While the ammonia leach and hydrogen reduction circuits were retained with only minor modifications, major changes were made in the processes for the separation and recovery of cobalt. A totally new cobaltnickel separation was successfully developed, in which most of the cobalt is separated from the ammoniacal nickel sulphate leach solution by precipitation as a cobalt-nickel hexammine salt, using anhydrous ammonia as the reagent. This salt, which contains equal amounts of cobalt and nickel, is refined to a pure cobaltic hexammine salt by selectively leaching nickel with water, and recrystallizing the resulting impure cobaltic hexammine salt in ammonium sulphate solution. The recrystallized cobalt hexammine salt has a Co : Ni ratio of over 2000 : 1, and contains very low levels of copper, zinc and cadmium. It is redissolved in ammonium sulphate solution and coverted to cobalt powder by hydrogen reduction. This paper describes the changes made to the refinery processes since 1991, and reviews recent operating performance with emphasis on the treatment of Moa sulphides.
机译:古巴的Moa Nickel S.A.从氧化铁皮红土矿石中生产的镍钴硫化物被运往加拿大的Corefco镍钴精炼厂。该精炼厂是位于艾伯塔省萨斯喀彻温堡的Sherritt Gordon镍精炼厂,自1954年以来一直在运营。需要对精炼工艺进行重大改动,以处理钴含量异常高的Moa硫化物原料。氨浸提和氢气还原回路保留了很小的改动,但在分离和回收钴的过程中进行了重大更改。成功开发了全新的钴镍分离方法,其中大部分钴通过使用无水氨水作为沉淀剂以钴镍六胺盐的形式从氨式硫酸镍浸出溶液中分离出来。通过选择性地用水浸出镍,然后在硫酸铵溶液中重结晶生成的不纯钴六胺盐,将该盐(包含等量的钴和镍)精炼成纯的钴六胺盐。重结晶的六方钴钴盐的Co:Ni比例超过2000:1,并且含有极少量的铜,锌和镉。将其重新溶解在硫酸铵溶液中,并通过氢还原将其覆盖成钴粉。本文介绍了自1991年以来炼油工艺的变化,并回顾了近期的经营业绩,重点是硫化莫亚胶的处理。

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