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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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Published in: | Minerals (Basel) 2023-11, Vol.13 (11), p.1372 |
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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− (0.1–0.3 M), pH 12–12.5; 20 to 40 °C, reaction time 0.5%As) into clean concentrates ( |
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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− (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)3, 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 Cl2 equivalent per kg of concentrate.</description><identifier>ISSN: 2075-163X</identifier><identifier>EISSN: 2075-163X</identifier><identifier>DOI: 10.3390/min13111372</identifier><language>eng</language><publisher>Basel: MDPI AG</publisher><subject>Analytical chemistry ; Arsenic ; Arsenic ions ; Chalcopyrite ; Chlorine ; Cleaning ; Cleaning process ; Consumption ; Copper ; copper concentrate ; Copper industry ; Enargite ; Ferric hydroxide ; hypochlorite medium ; Iodine ; Iron ; Leaching ; Metallurgy ; Microscopy ; Reagents ; Securities ; selective leaching ; Selectivity ; Smelters ; Sodium ; Sodium hypochlorite ; Solid phases ; Sulfur</subject><ispartof>Minerals (Basel), 2023-11, Vol.13 (11), p.1372</ispartof><rights>COPYRIGHT 2023 MDPI AG</rights><rights>2023 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (https://creativecommons.org/licenses/by/4.0/). Notwithstanding the ProQuest Terms and Conditions, you may use this content in accordance with the terms of the License.</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c403t-b2fb447d2faba74a33dddfd2c3d2844bb887cf2c53ec7eaa53197ea15c256dd63</citedby><cites>FETCH-LOGICAL-c403t-b2fb447d2faba74a33dddfd2c3d2844bb887cf2c53ec7eaa53197ea15c256dd63</cites><orcidid>0000-0001-8719-7560 ; 0000-0003-0610-0048 ; 0000-0001-6211-6082</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://www.proquest.com/docview/2893305498/fulltextPDF?pq-origsite=primo$$EPDF$$P50$$Gproquest$$Hfree_for_read</linktopdf><linktohtml>$$Uhttps://www.proquest.com/docview/2893305498?pq-origsite=primo$$EHTML$$P50$$Gproquest$$Hfree_for_read</linktohtml><link.rule.ids>314,780,784,11688,25753,27924,27925,36060,37012,44363,44590,74895,75126</link.rule.ids></links><search><creatorcontrib>Hernández, Maria Cecilia</creatorcontrib><creatorcontrib>Benavente, Oscar</creatorcontrib><creatorcontrib>Roca, Antoni</creatorcontrib><creatorcontrib>Melo, Evelyn</creatorcontrib><creatorcontrib>Quezada, Víctor</creatorcontrib><title>Selective Leaching of Arsenic from Copper Concentrates in Hypochlorite Medium</title><title>Minerals (Basel)</title><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− (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)3, 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 Cl2 equivalent per kg of concentrate.</description><subject>Analytical chemistry</subject><subject>Arsenic</subject><subject>Arsenic ions</subject><subject>Chalcopyrite</subject><subject>Chlorine</subject><subject>Cleaning</subject><subject>Cleaning process</subject><subject>Consumption</subject><subject>Copper</subject><subject>copper concentrate</subject><subject>Copper industry</subject><subject>Enargite</subject><subject>Ferric hydroxide</subject><subject>hypochlorite medium</subject><subject>Iodine</subject><subject>Iron</subject><subject>Leaching</subject><subject>Metallurgy</subject><subject>Microscopy</subject><subject>Reagents</subject><subject>Securities</subject><subject>selective leaching</subject><subject>Selectivity</subject><subject>Smelters</subject><subject>Sodium</subject><subject>Sodium hypochlorite</subject><subject>Solid 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Leaching of Arsenic from Copper Concentrates in Hypochlorite Medium</title><author>Hernández, Maria Cecilia ; Benavente, Oscar ; Roca, Antoni ; Melo, Evelyn ; Quezada, Víctor</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c403t-b2fb447d2faba74a33dddfd2c3d2844bb887cf2c53ec7eaa53197ea15c256dd63</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2023</creationdate><topic>Analytical chemistry</topic><topic>Arsenic</topic><topic>Arsenic ions</topic><topic>Chalcopyrite</topic><topic>Chlorine</topic><topic>Cleaning</topic><topic>Cleaning process</topic><topic>Consumption</topic><topic>Copper</topic><topic>copper concentrate</topic><topic>Copper industry</topic><topic>Enargite</topic><topic>Ferric hydroxide</topic><topic>hypochlorite 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in Hypochlorite Medium</atitle><jtitle>Minerals (Basel)</jtitle><date>2023-11-01</date><risdate>2023</risdate><volume>13</volume><issue>11</issue><spage>1372</spage><pages>1372-</pages><issn>2075-163X</issn><eissn>2075-163X</eissn><abstract>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− (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)3, 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 Cl2 equivalent per kg of concentrate.</abstract><cop>Basel</cop><pub>MDPI AG</pub><doi>10.3390/min13111372</doi><orcidid>https://orcid.org/0000-0001-8719-7560</orcidid><orcidid>https://orcid.org/0000-0003-0610-0048</orcidid><orcidid>https://orcid.org/0000-0001-6211-6082</orcidid><oa>free_for_read</oa></addata></record> |
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subjects | Analytical chemistry Arsenic Arsenic ions Chalcopyrite Chlorine Cleaning Cleaning process Consumption Copper copper concentrate Copper industry Enargite Ferric hydroxide hypochlorite medium Iodine Iron Leaching Metallurgy Microscopy Reagents Securities selective leaching Selectivity Smelters Sodium Sodium hypochlorite Solid phases Sulfur |
title | Selective Leaching of Arsenic from Copper Concentrates in Hypochlorite Medium |
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