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Improvement of Gold and Silver Recuperation from Low-Grade Solutions Through Mixed Process: Desorption Zadra and Merrill Crowe

机译:通过混合过程改善低档解决方案的黄金和白银回收:解吸扎拉德拉和美林群

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During beneficiation metallurgical plant operation different conditions can affect the process. These variations or new conditions often require modifications to operational criteria or complements of different processes to the actual, in order to maintain or improve production rates. In the present case study, a mining company in Peru, that exploits a low sulfidation epithermal Au-Ag deposit, uses a heap leaching process to extract the valuable minerals, and after that, recover them through precipitation technology with zinc called Merrill-Crowe. During the first years of operation, the content of Au and Ag dissolved in the solution were high, so the minerals were quickly recovered due to the first levels of the leaching pad. However, the increase in area, pad height and the irrigation of exhausted (aged) cells generated a low-grade Au- Ag solution (intermediate solution) in the transit of the percolation solution. This solution was mixed with the rich solution generating high flow to be treated in the Merrill Crowe plant, causing an increase in operating costs. A balance solutions study was realized to obtain Au-Ag content and flow rate that was economically unfeasible to be treated in Merrill-Crowe process plant but feasible to carry it to a recover process with less cost, using activated carbon (CIC).After several metallurgical tests, we concluded that it is necessary an adsorption plant through activated carbon in column (CIC) and desorption process (pressurized Zadra) to make possible recover the gold and silver of new solutions (low-grade solution). The concentrated solution from the Zadra recovery plant, produced from low-grade solutions, should enter to Merrill-Crowe plant and as a result, it would optimize the consumption of metallic zinc dust, thus obtain a cleaner precipitate for processing in foundry. Finally, beneficiation plant that has Merrill Crowe process, now has an activated carbon plant additionally.The project investment was 7.8 Mills US$ and the new plant produced 19,500 oz of gold and 155,000 oz of silver. The project obtained an NPV of 18.6 Mills US$, an IRR value of 100 % and a payback period of fifteen months.
机译:在受益期间,冶金工厂运行不同的条件会影响该过程。这些变体或新条件通常需要修改对实际过程的操作标准或补充,以便维护或提高生产率。在目前的案例研究中,秘鲁的矿业公司利用低硫化术术Au-Ag沉积物,采用堆浸出过程来提取有价值的矿物质,并在此之后通过锌的降水技术恢复,含有Merrill-Crowe的锌。在操作的第一年,溶解在溶液中的Au和Ag的含量高,因此由于浸出垫的第一级,矿物迅速恢复。然而,面积,垫高度和排出的(老年)细胞的灌溉的增加产生了渗透溶液的过渡中的低级Au-Ag溶液(中间溶液)。将该溶液与富溶液混合,产生高流量以在Merrill Crowe植物中处理,导致运营成本增加。实现了平衡解决方案研究,以获得Merrill-Crowe Process Plance在Merrill-Crowe Process Plance中经济地处理的Au-Ag含量和流量,但使用活性炭(CIC),可行的成本较低,以较低的成本将其携带到恢复过程中。冶金试验,我们得出结论,通过柱(CIC)和解吸过程(加压ZADRA)中通过活性炭进行吸附植物,以取回新溶液的金和银(低级溶液)。由低级溶液生产的ZADRA回收厂的浓缩溶液应进入Merrill-Crowe植物,结果,它将优化金属锌粉尘的消耗,从而获得铸造厂加工的清洁沉淀物。最后,拥有美林群体的惠矿工厂,现在还有一个活性炭植物。项目投资为7.8米,新工厂生产了19,500盎司的金,15.5万盎司的银。该项目获得了18.6毫克US $的NPV,额外价值100%和15个月的投资回收期。

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