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Hydrometallurgical Technology for Producing Rhenium(VII) and Cobalt(II) from Waste
This paper presents a method for obtaining cobalt(II) perrhenate from waste derived from two types of materials, i.e., Li-ion battery scrap, or more precisely, battery mass, and superalloy scrap. Both of the above-mentioned materials are a source of Co. However, a source of rhenium is perrhenic acid...
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Published in: | Crystals (Basel) 2024-09, Vol.14 (9), p.783 |
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creator | Leszczyńska-Sejda, Katarzyna Malarz, Joanna Ciszewski, Mateusz Kopyto, Dorota Goc, Karolina Grzybek, Alicja Kowalik, Patrycja Orda, Szymon Pianowska, Karolina Turczyńska, Aleksandra Benke, Grzegorz |
description | This paper presents a method for obtaining cobalt(II) perrhenate from waste derived from two types of materials, i.e., Li-ion battery scrap, or more precisely, battery mass, and superalloy scrap. Both of the above-mentioned materials are a source of Co. However, a source of rhenium is perrhenic acid produced from ammonium perrhenate (recycled) by the ion exchange method using resins. Co(OH)2 can be precipitated from solutions resulting from the leaching of Li-ion battery mass, sludge from the Zn-Pb industry and superalloy scrap. The compound, after proper purification, can be used in a reaction with perrhenic acid to form Co(ReO4)2. The reaction should be conducted under the following conditions: time 1 h, room temperature, 30% excess of cobalt(II) hydroxide, and rhenium concentration in HReO4 from about 20 g/dm3 to 300 g/dm3. This work shows that with the use of Co(OH)2, obtained from waste, an anhydrous form of cobalt(II) perrhenate can be obtained, containing < 1000 ppm of the cumulative metal impurities. |
doi_str_mv | 10.3390/cryst14090783 |
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Both of the above-mentioned materials are a source of Co. However, a source of rhenium is perrhenic acid produced from ammonium perrhenate (recycled) by the ion exchange method using resins. Co(OH)2 can be precipitated from solutions resulting from the leaching of Li-ion battery mass, sludge from the Zn-Pb industry and superalloy scrap. The compound, after proper purification, can be used in a reaction with perrhenic acid to form Co(ReO4)2. The reaction should be conducted under the following conditions: time 1 h, room temperature, 30% excess of cobalt(II) hydroxide, and rhenium concentration in HReO4 from about 20 g/dm3 to 300 g/dm3. This work shows that with the use of Co(OH)2, obtained from waste, an anhydrous form of cobalt(II) perrhenate can be obtained, containing < 1000 ppm of the cumulative metal impurities.</description><identifier>ISSN: 2073-4352</identifier><identifier>EISSN: 2073-4352</identifier><identifier>DOI: 10.3390/cryst14090783</identifier><language>eng</language><publisher>Basel: MDPI AG</publisher><subject>Aluminum ; Catalysis ; Cobalt ; Cobalt compounds ; Crystal structure ; Ion exchange ; Leaching ; Li-ion battery masses ; Lithium-ion batteries ; Nickel ; Oxidation ; Rhenium ; Room temperature ; Scrap ; Sulfuric acid ; Superalloys ; Temperature ; Zinc compounds</subject><ispartof>Crystals (Basel), 2024-09, Vol.14 (9), p.783</ispartof><rights>2024 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><cites>FETCH-LOGICAL-c256t-b0891e3bbc19730430f90ee2739d923ae29ec01f0bf3988455e078102ae126f93</cites><orcidid>0000-0001-9076-8301 ; 0000-0003-2039-5858 ; 0000-0001-9737-2887 ; 0000-0002-5850-1735 ; 0009-0006-3477-1294 ; 0009-0006-4101-6510 ; 0000-0002-3507-4195 ; 0000-0001-9847-3225 ; 0000-0002-3654-0039</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://www.proquest.com/docview/3110449715/fulltextPDF?pq-origsite=primo$$EPDF$$P50$$Gproquest$$Hfree_for_read</linktopdf><linktohtml>$$Uhttps://www.proquest.com/docview/3110449715?pq-origsite=primo$$EHTML$$P50$$Gproquest$$Hfree_for_read</linktohtml><link.rule.ids>314,780,784,25753,27924,27925,37012,44590,75126</link.rule.ids></links><search><creatorcontrib>Leszczyńska-Sejda, Katarzyna</creatorcontrib><creatorcontrib>Malarz, Joanna</creatorcontrib><creatorcontrib>Ciszewski, Mateusz</creatorcontrib><creatorcontrib>Kopyto, Dorota</creatorcontrib><creatorcontrib>Goc, Karolina</creatorcontrib><creatorcontrib>Grzybek, Alicja</creatorcontrib><creatorcontrib>Kowalik, Patrycja</creatorcontrib><creatorcontrib>Orda, Szymon</creatorcontrib><creatorcontrib>Pianowska, Karolina</creatorcontrib><creatorcontrib>Turczyńska, Aleksandra</creatorcontrib><creatorcontrib>Benke, Grzegorz</creatorcontrib><title>Hydrometallurgical Technology for Producing Rhenium(VII) and Cobalt(II) from Waste</title><title>Crystals (Basel)</title><description>This paper presents a method for obtaining cobalt(II) perrhenate from waste derived from two types of materials, i.e., Li-ion battery scrap, or more precisely, battery mass, and superalloy scrap. Both of the above-mentioned materials are a source of Co. However, a source of rhenium is perrhenic acid produced from ammonium perrhenate (recycled) by the ion exchange method using resins. Co(OH)2 can be precipitated from solutions resulting from the leaching of Li-ion battery mass, sludge from the Zn-Pb industry and superalloy scrap. The compound, after proper purification, can be used in a reaction with perrhenic acid to form Co(ReO4)2. The reaction should be conducted under the following conditions: time 1 h, room temperature, 30% excess of cobalt(II) hydroxide, and rhenium concentration in HReO4 from about 20 g/dm3 to 300 g/dm3. 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Both of the above-mentioned materials are a source of Co. However, a source of rhenium is perrhenic acid produced from ammonium perrhenate (recycled) by the ion exchange method using resins. Co(OH)2 can be precipitated from solutions resulting from the leaching of Li-ion battery mass, sludge from the Zn-Pb industry and superalloy scrap. The compound, after proper purification, can be used in a reaction with perrhenic acid to form Co(ReO4)2. The reaction should be conducted under the following conditions: time 1 h, room temperature, 30% excess of cobalt(II) hydroxide, and rhenium concentration in HReO4 from about 20 g/dm3 to 300 g/dm3. This work shows that with the use of Co(OH)2, obtained from waste, an anhydrous form of cobalt(II) perrhenate can be obtained, containing < 1000 ppm of the cumulative metal impurities.</abstract><cop>Basel</cop><pub>MDPI AG</pub><doi>10.3390/cryst14090783</doi><orcidid>https://orcid.org/0000-0001-9076-8301</orcidid><orcidid>https://orcid.org/0000-0003-2039-5858</orcidid><orcidid>https://orcid.org/0000-0001-9737-2887</orcidid><orcidid>https://orcid.org/0000-0002-5850-1735</orcidid><orcidid>https://orcid.org/0009-0006-3477-1294</orcidid><orcidid>https://orcid.org/0009-0006-4101-6510</orcidid><orcidid>https://orcid.org/0000-0002-3507-4195</orcidid><orcidid>https://orcid.org/0000-0001-9847-3225</orcidid><orcidid>https://orcid.org/0000-0002-3654-0039</orcidid><oa>free_for_read</oa></addata></record> |
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subjects | Aluminum Catalysis Cobalt Cobalt compounds Crystal structure Ion exchange Leaching Li-ion battery masses Lithium-ion batteries Nickel Oxidation Rhenium Room temperature Scrap Sulfuric acid Superalloys Temperature Zinc compounds |
title | Hydrometallurgical Technology for Producing Rhenium(VII) and Cobalt(II) from Waste |
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