Recovery of high-grade cobalt oxide from zinc plant residue (ZPR) generated at zinc processing plants

IF 4.8 2区 材料科学 Q1 METALLURGY & METALLURGICAL ENGINEERING
Sunil Kumar , Shavi Agrawal , Kiran Kumar Rokkam , Sudhakar Yadav , Raj Kumar Dishwar
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Abstract

In the present study, a method for cobalt recovery from Zinc Plant Residue (ZPR) has been developed. First, the residue was leached in a dilute sulfuric acid solution. >90% cobalt and 95% zinc were leached in two hours at room temperature. Then, leach liquor was purified before cobalt precipitation. First, copper and cadmium were removed using zinc dust. >99% copper and 80% cadmium were removed in 30 min at room temperature with slow agitation. Then, dissolved iron was removed using sodium persulfate as an oxidizing agent, and lime was used to maintain pH. Iron was precipitated (∼99%) in 1 h at 60 °C temperature by maintaining pH at 3.5 and Eh at 700 mV. After iron removal, cobalt was precipitated by using sodium persulfate as an oxidizing agent, and sodium hydroxide was used to maintain pH. The cobalt precipitate was calcined and then the final product was obtained with 58% Co. The filtrate, obtained after cobalt precipitation, had a zinc concentration of approximately 69 g/L. About 82% cobalt and 90% zinc were recovered in the entire process.

从锌加工厂产生的锌厂残渣(ZPR)中回收高品位氧化钴
本研究开发了一种从锌厂残渣(ZPR)中回收钴的方法。首先,在稀硫酸溶液中浸出锌渣。在室温下浸出两小时后,钴含量>90%,锌含量>95%。然后,在钴沉淀之前对浸出液进行净化。首先,使用锌粉去除铜和镉。在室温下缓慢搅拌 30 分钟后,>99% 的铜和 80% 的镉被去除。然后,用过硫酸钠作为氧化剂去除溶解的铁,并用石灰保持 pH 值。将 pH 值保持在 3.5,Eh 值保持在 700 mV,在 60 °C 温度下 1 小时内沉淀出铁(≥99%)。除铁后,用过硫酸钠作为氧化剂沉淀钴,并用氢氧化钠维持 pH 值。钴沉淀经煅烧后得到含钴量为 58% 的最终产品。钴沉淀后的滤液中锌浓度约为 69 克/升。整个过程回收了约 82% 的钴和 90% 的锌。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
Hydrometallurgy
Hydrometallurgy 工程技术-冶金工程
CiteScore
9.50
自引率
6.40%
发文量
144
审稿时长
3.4 months
期刊介绍: Hydrometallurgy aims to compile studies on novel processes, process design, chemistry, modelling, control, economics and interfaces between unit operations, and to provide a forum for discussions on case histories and operational difficulties. Topics covered include: leaching of metal values by chemical reagents or bacterial action at ambient or elevated pressures and temperatures; separation of solids from leach liquors; removal of impurities and recovery of metal values by precipitation, ion exchange, solvent extraction, gaseous reduction, cementation, electro-winning and electro-refining; pre-treatment of ores by roasting or chemical treatments such as halogenation or reduction; recycling of reagents and treatment of effluents.
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