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RECOVERY OF GOLD FROM THIOSULFATE SOLUTIONS AND PULPS WITH ION-EXCHANGE RESINS

机译:硫代硫酸盐溶液和纸浆中的离子交换树脂回收金

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Growing environmental and occupational safety concerns about the use of cyanide in gold processing has increased the interest in more acceptable alternatives. The most likely of these is thiosulfate. However, the thiosulfate process lacks a proven in-pulp method of recovering the dissolved gold, because activated carbon is not effective for the absorption of the gold thiosulfate complex. Anion exchange resins do offer a possible route for in-pulp recovery. This paper describes work aimed at the evaluation of the effectiveness of commercially available anion exchange resins for the recovery of gold from thiosulfate leach liquors and pulps. It has been found that strong-base resins are superior to weak-base resins in that they have a larger capacity, which assists in reducing the competition from other anions within a leach solution. Further studies with a selected commercial strong-base resin have shown that competing polythionate anions (particularly tri- and tetrathionate) lower the maximum possible gold loading but that gold is selectively recovered over other base metal anions in solution. Kinetic experiments found that while competing anions did not affect the initial rate of gold loading it was important to minimise the contact time of the resin in solution so to prevent displacement of loaded gold by competing anions over longer times. A small-scale resin-in-pulp plant investigation showed gold can be recovered from a leach pulp by a strong-base resin to yield gold loadings of 3000 mg/L, barren pulp containing less than 0.05 mg/L of dissolved gold and copper loadings of 500 mg/L. Loaded copper was displaced by gold and at a loading of 2000 mg/L gold the copper loading was minimal (<500 mg/L). The resin was found to recover gold adsorbed on the solids that would otherwise have reported to tails if a solid/liquid separation method were used. A patented two-step elution process in which copper and then gold are separately eluted from the resin is also discussed.
机译:有关在金加工中使用氰化物的环境和职业安全问题日益引起关注,这增加了人们对更可接受的替代品的兴趣。其中最可能的是硫代硫酸盐。但是,硫代硫酸盐工艺缺乏一种经过实践证明的纸浆中回收溶解金的方法,因为活性炭对硫代硫酸金络合物的吸收无效。阴离子交换树脂确实为纸浆中回收提供了可能的途径。本文介绍了旨在评估可商购的阴离子交换树脂从硫代硫酸盐浸出液和纸浆中回收金的有效性的工作。已经发现强碱树脂优于弱碱树脂之处在于它们具有更大的容量,这有助于减少浸出溶液中与其他阴离子的竞争。对选定的市售强碱树脂的进一步研究表明,竞争的多硫氰酸盐阴离子(尤其是三和四硫氰酸盐)降低了最大可能的金负载量,但与溶液中的其他贱金属阴离子相比,有选择地回收了金。动力学实验发现,尽管竞争阴离子不会影响金的初始加载速率,但重要的是使树脂在溶液中的接触时间最短,从而防止竞争阴离子长时间吸附负载的金。一项小规模的纸浆树脂工厂调查显示,可以通过强碱树脂从浸出纸浆中回收金,从而产生3000 mg / L的金负载量,贫浆中的溶解金和铜含量低于0.05 mg / L载量为500 mg / L。负载的铜被金置换,在金的负载为2000 mg / L时,铜的负载最小(<500 mg / L)。发现该树脂回收了吸附在固体上的金,如果使用固/液分离方法,则该金否则会报告为尾巴。还讨论了获得专利的两步洗脱方法,其中铜和金分别从树脂中洗脱出来。

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