Study on pre-oxidation of silver concentrate and leaching behaviour of Zn, Cu and In during oxygen-pressure leaching

IF 4.8 2区 材料科学 Q1 METALLURGY & METALLURGICAL ENGINEERING
Liu Qiang, Li Cun-xiong , Gu Zhi-hui, Li Chang-wen, Wang Qi-liang
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引用次数: 0

Abstract

Given the limitations of current processing methods and the potential of high recovery of silver as a flotation concentrate, this study proposes a pre-oxidation followed by oxygen pressure sulphuric acid leaching route for zinc, copper and indium and thoroughly examines the alteration in micro-morphology of the silver concentrate of 1.22% Pb, 3010 g/t Ag and 649 g/t In. Under the optimal conditions of a sulphuric acid pre-oxidation temperature of 60 °C, and an acid-to-ore mass ratio of 0.6, over 15 h, the PO and -OH polar groups of flotation reagents on the surface of silver concentrate particles are effectively neutralized through sulphuric acid oxidation. This action prevents the formation of a hydration film and mineral inclusions, thereby facilitating the efficient leaching of valuable elements. With a set reaction temperature of 155 °C, an initial acidity of 160 g/L, a reaction time of 180 min, an oxygen partial pressure of 0.8 MPa and a liquid-to-solid ratio of 7 mL/g, the leaching efficiency of Zn, Cu and In in the silver concentrate reach 94.8%, 98.4% and 91.1%, respectively while the lead and silver grades in the leach residue increase to 2.88% and 7754 g/t, respectively.

银精矿预氧化及氧压浸出过程中锌、铜和铟的浸出行为研究
考虑到当前处理方法的局限性和浮选精矿中银的高回收率潜力,本研究提出了一条先预氧化后氧压硫酸浸出锌、铜和铟的路线,并深入研究了铅含量为 1.22%、银含量为 3010 g/t 和铟含量为 649 g/t 的银精矿的微观形态变化。在硫酸预氧化温度为 60 °C、酸矿质量比为 0.6 的最佳条件下,经过 15 小时的硫酸氧化,银精矿颗粒表面浮选试剂的 PO 和 -OH 极性基团被有效中和。这种作用可防止形成水化膜和矿物夹杂物,从而促进有价元素的有效沥滤。在设定反应温度为 155 ℃、初始酸度为 160 g/L、反应时间为 180 分钟、氧分压为 0.8 MPa 和液固比为 7 mL/g 的条件下,银精矿中锌、铜和铟的浸出效率分别达到 94.8%、98.4% 和 91.1%,而浸出残渣中的铅和银品位则分别提高到 2.88% 和 7754 g/t。
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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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