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OPTIONS OF GOLD AND COPPER RECOVERY FROM GLYCINE AND GLYCINE-CYANIDE SOLUTIONS

机译:来自甘氨酸和甘氨酸 - 氰化物溶液的金和铜回收的选择

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The glycine based technology for gold and copper leaching was invented and patented at Curtin University in 2013. Leaching gold in starved or low cyanide solutions in the presence of glycine and an oxidant significantly improved the gold recovery and reduced the cyanide consumption (GlyCat? Process). The glycine-only system (GlyLeach~(TM)) can also effectively leach copper and other base metals such as nickel, cobalt, zinc and lead.The downstream processing of solutions from the leaching of copper and copper bearing gold ores in different glycine leach systems is critical for the successful implementation of the new leach system at an industrial scale.This paper outlines the successful options for copper and gold recovery from both glycine and glycine-cyanide solutions. The use of solvent extraction, sulfide precipitation, and ion exchange resins for copper recovery were tested, while activated carbon and ion exchange resins were used to evaluate the gold recovery from glycine solutions. More than 99% of copper was recovered as covellite by sulphide precipitation. Solvent extraction results showed that copper glycinate at alkaline pH (pH 10.0) can be easily loaded onto LIX84 extractant followed by sulphuric acid stripping. Chelating ion exchange resins efficiently and selectively adsorbed the cupric copper over gold complexes from alkaline glycine solutions. After the copper recovery by sulphide precipitation, ion exchange or solvent extraction, it was shown that the complexed glycine with the cupric ions was released back to the leach solutions and does not adsorb onto the extractants or precipitates. It was also seen that the activated carbon had a high adsorption tendency towards gold over copper from glycine-cyanide solutions. The gold and copper adsorption on carbon from a cyanide-glycine solution containing 2 mg/L gold, 300 mg/L copper, pH 11, 5 g/L glycine, Cu:CN of 1:1 (123 mg/L CN) and 8 g/L carbon in 24 hours reached 99.0% and 52.8% respectively. Activated carbon was found to be very selective for gold glycinate over cupric glycinate from glycine only solutions. More than 99.0% gold was adsorbed in 24 hours and less than 15% copper was adsorbed at the same time under optimum conditions from a glycine solution containing 7.5 g/L glycine, 2 ppm gold and 40 ppm copper.The optimum process for copper and gold recovery from glycine-cyanide solutions was found to be an initial copper recovery by either sulphide precipitation or ion exchange resin followed by gold recovery with activated carbon.
机译:2013年Curtin University的甘氨酸基金和铜浸出技术在甘氨酸和低氰化物溶液中的浸出金在甘氨酸和氧化剂存在下显着改善了黄金恢复并降低了氰化物消耗(甘露糖?工艺) 。仅甘氨酸系统(Glyleach〜(TM))也可以有效地浸出铜和其他基础金属,例如镍,钴,锌和铅。来自铜和铜轴承金矿浸出的溶液的下游加工在不同的甘氨酸浸出中系统对于在工业规模成功实施新的浸出系统至关重要。本文概述了甘氨酸和甘氨酸 - 氰化物溶液中铜和金回收的成功选择。测试溶剂萃取,硫化物沉淀和离子交换树脂进行铜回收,而活性炭和离子交换树脂用于评估从甘氨酸溶液中的金回收。通过硫化物沉淀将超过99%的铜回收铜。溶剂萃取结果表明,碱性pH(pH1.10.0)的铜甘油酸铜可以容易地装载到Lix84萃取剂上,然后硫酸剥离。螯合离子交换有效树脂,并选择性地吸附来自碱性甘氨酸溶液的金络合物上的铜铜。通过硫化物沉淀的铜回收,离子交换或溶剂萃取后,显示络合物甘氨酸与铜离子释放回浸出溶液,并不吸附到萃取剂上或沉淀物。还可以看出,活性炭对来自甘氨酸 - 氰化物溶液的铜的金具有高吸附倾向。来自含有2mg / L金,300mg / L铜,pH11,5g / L甘氨酸,Cn:Cn为1:1(123mg / L CN)和1:1(123mg / L)和1:1的碳铜溶液对碳的金和铜吸附碳上的碳和铜吸附。 24小时内的8克/升碳分别达到99.0%和52.8%。发现活性炭对于从甘氨酸甘氨酸的铜甘氨酸盐上的金甘氨酸非常有选择性。在24小时内吸附超过99.0%的金,在含有7.5g / l甘氨酸的甘氨酸溶液,2ppm金和40ppm铜的甘氨酸溶液中同时吸附超过15%的铜。铜和铜的最佳方法发现从甘氨酸 - 氰化物溶液中的金回收是通过硫化物沉淀或离子交换树脂的初始铜回收,然后用活性炭回收金。

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