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Enhanced leachability of gold and silver in cyanide media: Effect of alkaline pre-treatment of jarosite minerals

机译:氰化物介质中金和银的增强浸出性:黄铁矿矿物的碱性预处理的效果

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Composite samples of tailings containing gold (1.35 g/t) and significant amounts of silver (155 g/t) were subjected to batchwise cyanide leaching to assess the feasibility of extracting gold and silver. The tailings are waste solids arising from flotation and leaching operations whereby the flotation product (sphalerite concentrate) is calcined and then solubilised into dilute sulphuric acid solution and eventually sequestered from the electrolyte by electrowinning. Silver and gold are part of the zinc refinery residue, flotation tailings and to a limited extent the calcine leach tailings. Mineralogical results showed that composite tailings are refractory in nature (44 percent quartz, 17 percent silico aluminates and 12 percent jarosites). The concept of enhancing gold and silver recovery from the tailings focused on firstly decomposing the jarosite minerals by alkaline pre-treatment and then secondly leaching with cyanide solution. These two steps ensured that free gold and silver found in the zinc refinery residue and in the jarosite minerals could be leached simultaneously. The composite tailings were treated with Ca(OH)_2 solutions and then heated to 90 deg C for 2 h to decompose the silver-bearing mineral (Ag,PbFe_3(SO_4)_2(OH)_6). The alkaline pre-treated tailings were then subjected to cyanide leach tests at different NaCN dosages (2.5-10 kg/t) and particle size (96-200 mu m). Without an alkaline pre-treatment stage, leach efficiencies achieved were 41 percent and 25 percent for gold and silver, respectively at 40 deg C and 8 h mixing time. But, better leach efficiencies (55 percent for Au, 81 percent for Ag) were achieved after the feed was pre-treated with Ca(OH)_2. The leaching mechanism of gold was explained by the shrinking sphere model denoted by surface chemical reaction.
机译:对含金(1.35 g / t)和大量银(155 g / t)的尾矿的复合样品进行分批氰化物浸提,以评估提取金和银的可行性。尾矿是浮选和浸出操作产生的废固体,其中将浮选产物(闪锌矿精矿)煅烧,然后溶解成稀硫酸溶液,最后通过电解沉积从电解质中分离出来。银和金是锌精炼厂残渣,浮选尾矿的一部分,在一定程度上是煅烧浸出尾矿的一部分。矿物学结果表明,复合尾矿本质上是难熔的(44%的石英,17%的硅酸铝和12%的钾铝石)。提高尾矿中金和银回收率的概念首先在于通过碱性预处理分解黄钾铁矾矿物,然后再用氰化物溶液浸出。这两个步骤确保了可以同时浸提锌提炼残渣和黄钾铁矾矿物中的游离金和银。将复合尾矿用Ca(OH)_2溶液处理,然后加热到90摄氏度,保持2小时,以分解含银矿物(Ag,PbFe_3(SO_4)_2(OH)_6)。然后将碱性预处理的尾矿以不同的NaCN剂量(2.5-10 kg / t)和粒径(96-200μm)进行氰化物浸出试验。如果不进行碱预处理阶段,则在40℃和8小时的混合时间下,金和银的浸出效率分别为41%和25%。但是,在用Ca(OH)_2预处理进料后,可获得更好的浸出效率(Au为55%,Ag为81%)。通过表面化学反应表示的收缩球模型解释了金的浸出机理。

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