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Dual lixiviant leaching process for extraction and recovery of gold from ores at room temperature

机译:在室温下从矿石中提取和回收金的双重浸滤浸出工艺

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A comprehensive investigation of Au leaching from gold ores with a solution containing thiourea and ammonium thiocyanate was performed. A goldore Awith18g/t of Au and 1.l5 wt.% of sulfur and another gold ore B with 55.7 g/t of Au and 11.67 wt.% of sulfur were used. The percentages of extracted Au were 57%, 66% and 95% for the leaching solutions containing thiourea only, ammonium thiocyanate only and ammonium thiocyanate plus thiourea, respectively, under optimal conditions. There were some interactions among thiourea, ammonium thiocyanate and ferric ion, which affected gold extraction greatly. The addition of thiocyanate reduced greatly the consumption of thiourea and the process cost accordingly. The optimal concentrations of thiourea, ammonium thiocyanate and ferric sulfate for ore A leaching were 0.13 M, 0.78 M and 0.028 M, respectively. The optimal pH, temperature, time, ratio of liquid to solid, agitation speed and particle size for ore A leaching were 1.5,21℃ , 6 h, 10,250 rpm and 54-74 urn, respectively. Au extraction for ore A was 95% under above optimal conditions. Au extraction was 97% when sulfur content of ore B was 1.48 wt.%. The preferential consumption of ferric ions by pyrite over by gold was the main reason for resulting in the decrease of gold extraction. Desulfurization is necessary to achieve a high gold extraction for this leaching system of thiourea-thiocynate-Fe3 +. After Au extraction, about 90% of Au was recovered as insoluble metallic Au by cementation using 5 g/L of Al powder. The cementation filtrate was reused to leach Au ore and about 91% of Au was extracted after pH adjustment. Thus, thiocyanate and thiourea could be reused, which reduced the process cost The leaching speed of Au of this method was more than 4 times faster than that of cyanidation process. This process concerning extraction and recovery of Au from Au ore was effective, fast, environmentally friendly and also likely economical.
机译:对含硫脲和硫氰酸铵的溶液从金矿石中浸出金进行了综合研究。使用具有18g / t的Au和1.15重量%的硫的金矿石A和具有55.7g / t的Au和11.67重量%的硫的另一金矿石B。在最佳条件下,仅含硫脲,仅硫氰酸铵和硫氰酸铵加硫脲的浸出溶液中提取的金的百分比分别为57%,66%和95%。硫脲,硫氰酸铵和三价铁离子之间存在一些相互作用,极大地影响了金的提取。硫氰酸盐的添加大大降低了硫脲的消耗和相应的加工成本。矿石A浸出的硫脲,硫氰酸铵和硫酸铁的最佳浓度分别为0.13 M,0.78 M和0.028M。矿石A浸出的最佳pH值,温度,时间,液固比,搅拌速度和粒度分别为1.5.21℃,6 h,10,250 rpm和54-74 urn。在上述最佳条件下,矿石A的金提取率为95%。当矿石B的硫含量为1.48重量%时,Au提取为97%。黄铁矿优先消耗铁离子而不是金优先消耗是导致金提取减少的主要原因。对于该硫脲-硫氰酸盐-Fe3 +的浸出系统,脱硫对于实现高金提取是必要的。在提取Au之后,通过使用5g / L的Al粉进行胶结,回收了约90%的Au作为不溶性金属Au。胶结滤液被再利用以浸出金矿石,并在调节pH后提取约91%的金。因此,硫氰酸盐和硫脲可以重复使用,从而降低了工艺成本。该方法金的浸出速度比氰化法快4倍以上。该关于从金矿石中提取和回收金的方法是有效,快速,环境友好的并且也可能是经济的。

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