Leaching Chalcocite in Chloride Media—A Review

Chalcocite is the most abundant secondary copper sulfide globally, with the highest copper content, and is easily treated by conventional hydrometallurgical processes, making it a very profitable mineral for extraction. Among the various leaching processes to treat chalcocite, chloride media show be...

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Autores principales: Norman Toro, Carlos Moraga, David Torres, Manuel Saldaña, Kevin Pérez, Edelmira Gálvez
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Lenguaje:EN
Publicado: MDPI AG 2021
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Acceso en línea:https://doaj.org/article/d56471c37eb34391ba962ec7231d2f3b
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spelling oai:doaj.org-article:d56471c37eb34391ba962ec7231d2f3b2021-11-25T18:26:12ZLeaching Chalcocite in Chloride Media—A Review10.3390/min111111972075-163Xhttps://doaj.org/article/d56471c37eb34391ba962ec7231d2f3b2021-10-01T00:00:00Zhttps://www.mdpi.com/2075-163X/11/11/1197https://doaj.org/toc/2075-163XChalcocite is the most abundant secondary copper sulfide globally, with the highest copper content, and is easily treated by conventional hydrometallurgical processes, making it a very profitable mineral for extraction. Among the various leaching processes to treat chalcocite, chloride media show better results and have a greater industrial boom. Chalcocite dissolution is a two-stage process, the second being much slower than the first. During the second stage, in the first instance, it is possible to oxidize the covellite in a wide range of chloride concentrations or redox potentials (up to 75% extraction of Cu). Subsequently, CuS<sub>2</sub> is formed, which is to be oxidized. It is necessary to work at high concentrations of chloride (>2.5 mol/L) and/or increase the temperature to reach a redox potential of over 650 mV, which in turn decreases the thickness of the elemental sulfur layer on the mineral surface, facilitating chloride ions to generate a better porosity of this. Finally, it is concluded that the most optimal way to extract copper from chalcocite is, during the first stage, to work with high concentrations of chloride (50–100 g/L) and low concentrations of sulfuric acid (0.5 mol/L) at a temperature environment, as other variables become irrelevant during this stage if the concentration of chloride ions in the system is high. While in the second stage, it is necessary to increase the temperature of the system (moderate temperatures) or incorporate a high concentration of some oxidizing agent to avoid the passivation of the mineral.Norman ToroCarlos MoragaDavid TorresManuel SaldañaKevin PérezEdelmira GálvezMDPI AGarticleCu<sub>2</sub>SCuSdissolutionchlorideMineralogyQE351-399.2ENMinerals, Vol 11, Iss 1197, p 1197 (2021)
institution DOAJ
collection DOAJ
language EN
topic Cu<sub>2</sub>S
CuS
dissolution
chloride
Mineralogy
QE351-399.2
spellingShingle Cu<sub>2</sub>S
CuS
dissolution
chloride
Mineralogy
QE351-399.2
Norman Toro
Carlos Moraga
David Torres
Manuel Saldaña
Kevin Pérez
Edelmira Gálvez
Leaching Chalcocite in Chloride Media—A Review
description Chalcocite is the most abundant secondary copper sulfide globally, with the highest copper content, and is easily treated by conventional hydrometallurgical processes, making it a very profitable mineral for extraction. Among the various leaching processes to treat chalcocite, chloride media show better results and have a greater industrial boom. Chalcocite dissolution is a two-stage process, the second being much slower than the first. During the second stage, in the first instance, it is possible to oxidize the covellite in a wide range of chloride concentrations or redox potentials (up to 75% extraction of Cu). Subsequently, CuS<sub>2</sub> is formed, which is to be oxidized. It is necessary to work at high concentrations of chloride (>2.5 mol/L) and/or increase the temperature to reach a redox potential of over 650 mV, which in turn decreases the thickness of the elemental sulfur layer on the mineral surface, facilitating chloride ions to generate a better porosity of this. Finally, it is concluded that the most optimal way to extract copper from chalcocite is, during the first stage, to work with high concentrations of chloride (50–100 g/L) and low concentrations of sulfuric acid (0.5 mol/L) at a temperature environment, as other variables become irrelevant during this stage if the concentration of chloride ions in the system is high. While in the second stage, it is necessary to increase the temperature of the system (moderate temperatures) or incorporate a high concentration of some oxidizing agent to avoid the passivation of the mineral.
format article
author Norman Toro
Carlos Moraga
David Torres
Manuel Saldaña
Kevin Pérez
Edelmira Gálvez
author_facet Norman Toro
Carlos Moraga
David Torres
Manuel Saldaña
Kevin Pérez
Edelmira Gálvez
author_sort Norman Toro
title Leaching Chalcocite in Chloride Media—A Review
title_short Leaching Chalcocite in Chloride Media—A Review
title_full Leaching Chalcocite in Chloride Media—A Review
title_fullStr Leaching Chalcocite in Chloride Media—A Review
title_full_unstemmed Leaching Chalcocite in Chloride Media—A Review
title_sort leaching chalcocite in chloride media—a review
publisher MDPI AG
publishDate 2021
url https://doaj.org/article/d56471c37eb34391ba962ec7231d2f3b
work_keys_str_mv AT normantoro leachingchalcociteinchloridemediaareview
AT carlosmoraga leachingchalcociteinchloridemediaareview
AT davidtorres leachingchalcociteinchloridemediaareview
AT manuelsaldana leachingchalcociteinchloridemediaareview
AT kevinperez leachingchalcociteinchloridemediaareview
AT edelmiragalvez leachingchalcociteinchloridemediaareview
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