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青海某蚀变岩型含金多金属矿石选矿试验研究

Experimental study on beneficiation of an altered rock-type gold-bearing polymetallic ore from Qinghai Province

  • 摘要: 青海某蚀变岩型含金多金属矿石中铅、锌矿物主要为硫化矿,粒度较粗,较易选别回收;金矿物主要为含银自然金、银金矿,以及少量金银矿,粒度微细,部分金矿物与方铅矿、闪锌矿、黄铁矿等金属矿物和脉石矿物嵌布关系密切,单体解离困难。基于工艺矿物学研究结果,为确保金、银高效回收,同时兼顾铅、锌、硫综合回收利用,进行了矿石先浮后浸和先浸后浮2种工艺方案的对比试验研究。结果显示,先浸后浮工艺的指标优于先浮后浸工艺。采用先浸后浮工艺,矿石全泥浸出金浸出率为86.31 %,银浸出率为33.58 %。浸渣浮选得到的铅精矿含金5.61 g/t、含银283 g/t、含铅59.68 %,金回收率4.08 %、银回收率53.64 %、铅回收率86.69 %;锌精矿含锌40.16 %,锌回收率52.00 %;硫精矿含硫44.23 %,硫回收率70.36 %。矿石全泥浸出+铅精矿金总回收率90.39 %,银总回收率87.22 %。采用先浸后浮工艺流程,可在高效回收贵金属金、银的同时,得到达到品位要求的铅精矿、锌精矿、硫精矿产品,实现了金、银、铅、锌、硫综合回收最大化。

     

    Abstract: In an altered rock-type gold-bearing polymetallic ore from Qinghai Province, lead and zinc minerals are predominantly sulfides with coarse grain size, making them relatively easy to recover by beneficiation. Gold minerals mainly consist of silver-bearing native gold, electrum, and a small amount of kustelite with fine particle size. Part of gold minerals is closely associated with metallic minerals such as galena, sphalerite, and pyrite, as well as gangue minerals, leading to difficult liberation. Based on the process mineralogy study results, comparative experiments were conducted on two process schemes, namely flotation followed by leaching and leaching followed by flotation, to ensure efficient recovery of gold and silver while also achieving comprehensive recovery and utilization of lead, zinc, and sulfur. The results show that the leaching followed by the flotation process outperforms the flotation followed by the leaching process. By using the leaching followed by flotation process, the whole-ore cyanidation leaching achieves a gold leaching rate of 86.31 % and a silver leaching rate of 33.58 %. From the flotation of the leaching residue, a lead concentrate is obtained containing 5.61 g/t Au, 283 g/t Ag, and 59.68 % Pb, with recoveries of 4.08 % for Au, 53.64 % for Ag, and 86.69 % for Pb, as well as a zinc concentrate containing 40.16 % Zn with a zinc recovery of 52.00 % and a sulfur concentrate containing 44.23 % S with a sulfur recovery of 70.36 %. The total gold recovery from whole-ore cyanidation leaching plus the lead concentrate is 90.39 %, and the total silver recovery is 87.22 %. The leaching followed by the flotation process achieves efficient recovery of the precious metals gold and silver while simultaneously producing lead, zinc, and sulfur concentrates that meet grade requirements, thereby maximizing the comprehensive recovery of gold, silver, lead, zinc, and sulfur.

     

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