Gold recovery from cyanidation residue by chloride leaching and carbon adsorption – Preliminary results from CICL process

IF 4.8 2区 材料科学 Q1 METALLURGY & METALLURGICAL ENGINEERING Hydrometallurgy Pub Date : 2024-04-08 DOI:10.1016/j.hydromet.2024.106304
Anssi Karppinen, Sipi Seisko, Laura Nevatalo, Benjamin P. Wilson, Kirsi Yliniemi, Mari Lundström
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Abstract

There is a vast amount of globally underutilized low-grade mine tailings and leach residues, including those from primary processing of gold. In this research, the target is to recover the remaining gold (10.9 g/t) from weathered refractory iron-rich residue that had previously been subject to autoclave oxidation, subsequent cyanidation in a conventional carbon-in-leach (CIL) circuit as well as storage at tailings area. Chloride leaching has been considered as one of the most promising cyanide-free gold leaching methods and it has shown positive outcomes in treating primary gold ores, concentrates, and flotation tailings. Therefore, in the current study, the iron-rich residue investigated was subjected to chloride leaching combined with simultaneous carbon adsorption. The investigated parameters included leaching time (2–8 h), chloride concentration ([Cl] = 0.2–5 M), type and concentration of oxidant ([Cu2+]/[Fe3+] = 0.1–1 M), as well as type and concentration of activated carbon (14–25 g/L), whereas S/L ratio (100 g/L), acidity (pH = 1), and temperature (90 °C) were kept constant. Leaching results indicate that up to 40% of the remaining gold could still be recovered from the investigated residue with optimized chloride leaching. According to the results, the most important parameter for gold recovery was the leaching time. Moreover, of the studied oxidants, cupric ions were shown to contribute more to gold recovery when compared to ferric ions (35% vs. 24% at [Cu2+]/[Fe3+] = 0.1 M). Nevertheless, an increase of cupric concentration from 0.1 M (low-concentrated) to 0.5 M, resulted in only a slight increase in gold recovery (from 36% to 40%), whereas no further improvement in gold recovery was achieved with a 1 M cupric concentration. Two studied activated carbon products showed equal effectiveness in gold adsorption. In-situ carbon adsorption was shown to occur effectively in chloride media, as all dissolved gold could be detected in the activated carbon, and the concentration of remaining gold in the pregnant leach solution was minimal (< 0.02 mg/L). These findings indicate that low-concentrated chloride leaching of leach residues from industrial gold processes can allow an enhanced recovery of gold from previously mined and treated raw materials.

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通过氯化物浸出和碳吸附从氰化残渣中回收黄金 - CICL 工艺的初步结果
全球有大量未得到充分利用的低品位矿山尾矿和浸出残渣,包括黄金初级加工过程中产生的尾矿和浸出残渣。在这项研究中,我们的目标是从风化难处理富铁残渣中回收剩余的黄金(10.9 克/吨),这些残渣之前曾被高压釜氧化,随后在传统的碳浸出(CIL)回路中进行氰化,并储存在尾矿区。氯化物浸出法被认为是最有前途的无氰浸金方法之一,在处理原生金矿石、精矿和浮选尾矿方面取得了积极成果。因此,在本研究中,对富含铁的残渣进行了氯化浸出并同时进行了碳吸附。研究参数包括浸出时间(2-8 h)、氯化物浓度([Cl-] = 0.2-5 M)、氧化剂类型和浓度([Cu2+]/[Fe3+] = 0.1-1 M)以及活性炭类型和浓度(14-25 g/L),而 S/L 比(100 g/L)、酸度(pH = 1)和温度(90 °C)保持不变。浸出结果表明,通过优化氯化物浸出,仍可从所研究的残渣中回收高达 40% 的剩余金。结果表明,金回收最重要的参数是浸出时间。此外,在所研究的氧化剂中,与铁离子相比,铜离子对金回收的贡献更大([Cu2+]/[Fe3+] = 0.1 M 时,35% 对 24%)。然而,铜离子浓度从 0.1 M(低浓度)增加到 0.5 M 时,金的回收率仅略有提高(从 36% 提高到 40%),而铜离子浓度达到 1 M 时,金的回收率没有进一步提高。所研究的两种活性炭产品对金的吸附效果相当。在氯化物介质中,原位碳吸附被证明是有效的,因为所有溶解的金都能在活性碳中检测到,而且孕浸溶液中剩余金的浓度极低(0.02 毫克/升)。这些研究结果表明,低浓度氯化物沥滤工业金加工过程中的沥滤残留物可以提高从以前开采和处理过的原材料中回收金的能力。
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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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