Selective Leaching of Arsenic from Copper Concentrates in Hypochlorite Medium

The selective leaching of arsenic using sodium hypochlorite was evaluated in order to reduce its concentration in a copper concentrate. The best conditions achieved in the synthetic concentrate were applied to the industrial concentrate. First, the individual behaviors of pure samples of enargite an...

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Main Authors: Maria Cecilia Hernández, Oscar Benavente, Antoni Roca, Evelyn Melo, Víctor Quezada
Format: Article
Language:English
Published: MDPI AG 2023-10-01
Series:Minerals
Subjects:
Online Access:https://www.mdpi.com/2075-163X/13/11/1372
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author Maria Cecilia Hernández
Oscar Benavente
Antoni Roca
Evelyn Melo
Víctor Quezada
author_facet Maria Cecilia Hernández
Oscar Benavente
Antoni Roca
Evelyn Melo
Víctor Quezada
author_sort Maria Cecilia Hernández
collection DOAJ
description The selective leaching of arsenic using sodium hypochlorite was evaluated in order to reduce its concentration in a copper concentrate. The best conditions achieved in the synthetic concentrate were applied to the industrial concentrate. First, the individual behaviors of pure samples of enargite and chalcopyrite were evaluated under a hypochlorite medium. The enargite reaction is significantly faster than chalcopyrite, allowing for greater selectivity to ClO<sup>−</sup> (0.1–0.3 M), pH 12–12.5; 20 to 40 °C, reaction time <60 min. Under these conditions, the reagent consumption for pure compounds approaches the stoichiometric consumption and presents a selectivity factor of 5/1. Furthermore, concentrate leaching in a sodium hypochlorite medium, containing enargite, releases arsenic ions into the solution, while copper and iron remain in the solid phase, as CuO and Fe(OH)<sub>3</sub>, respectively. A novel copper concentrate cleaning process by selective leaching is proposed, which transforms unacceptable copper concentrate for smelters (>0.5%As) into clean concentrates (<0.2%As) or low penalty concentrates (0.2 < %As < 0.5). The estimated consumption for the cleaning process is in the order of 0.4–0.6 kg Cl<sub>2</sub> equivalent per kg of concentrate.
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spelling doaj.art-ec939855eab843f48fd0fa4cf54e24c12023-11-24T14:57:27ZengMDPI AGMinerals2075-163X2023-10-011311137210.3390/min13111372Selective Leaching of Arsenic from Copper Concentrates in Hypochlorite MediumMaria Cecilia Hernández0Oscar Benavente1Antoni Roca2Evelyn Melo3Víctor Quezada4Metallurgical and Mining Engineering Department, Universidad Católica del Norte, Antofagasta 1240000, ChileMetallurgical and Mining Engineering Department, Universidad Católica del Norte, Antofagasta 1240000, ChileDepartment of Materials Science and Physical Chemistry, Universitat de Barcelona, 08007 Barcelona, SpainMetallurgical and Mining Engineering Department, Universidad Católica del Norte, Antofagasta 1240000, ChileMetallurgical and Mining Engineering Department, Universidad Católica del Norte, Antofagasta 1240000, ChileThe selective leaching of arsenic using sodium hypochlorite was evaluated in order to reduce its concentration in a copper concentrate. The best conditions achieved in the synthetic concentrate were applied to the industrial concentrate. First, the individual behaviors of pure samples of enargite and chalcopyrite were evaluated under a hypochlorite medium. The enargite reaction is significantly faster than chalcopyrite, allowing for greater selectivity to ClO<sup>−</sup> (0.1–0.3 M), pH 12–12.5; 20 to 40 °C, reaction time <60 min. Under these conditions, the reagent consumption for pure compounds approaches the stoichiometric consumption and presents a selectivity factor of 5/1. Furthermore, concentrate leaching in a sodium hypochlorite medium, containing enargite, releases arsenic ions into the solution, while copper and iron remain in the solid phase, as CuO and Fe(OH)<sub>3</sub>, respectively. A novel copper concentrate cleaning process by selective leaching is proposed, which transforms unacceptable copper concentrate for smelters (>0.5%As) into clean concentrates (<0.2%As) or low penalty concentrates (0.2 < %As < 0.5). The estimated consumption for the cleaning process is in the order of 0.4–0.6 kg Cl<sub>2</sub> equivalent per kg of concentrate.https://www.mdpi.com/2075-163X/13/11/1372copper concentrateselective leachingenargitehypochlorite medium
spellingShingle Maria Cecilia Hernández
Oscar Benavente
Antoni Roca
Evelyn Melo
Víctor Quezada
Selective Leaching of Arsenic from Copper Concentrates in Hypochlorite Medium
Minerals
copper concentrate
selective leaching
enargite
hypochlorite medium
title Selective Leaching of Arsenic from Copper Concentrates in Hypochlorite Medium
title_full Selective Leaching of Arsenic from Copper Concentrates in Hypochlorite Medium
title_fullStr Selective Leaching of Arsenic from Copper Concentrates in Hypochlorite Medium
title_full_unstemmed Selective Leaching of Arsenic from Copper Concentrates in Hypochlorite Medium
title_short Selective Leaching of Arsenic from Copper Concentrates in Hypochlorite Medium
title_sort selective leaching of arsenic from copper concentrates in hypochlorite medium
topic copper concentrate
selective leaching
enargite
hypochlorite medium
url https://www.mdpi.com/2075-163X/13/11/1372
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