Analysis of Lanthanum and Cobalt Leaching Aimed at Effective Recycling Strategies of Solid Oxide Cells
Lanthanum and cobalt are Critical Raw Materials and components of Solid Oxide Cells—SOCs electrodes. This review analyses lanthanum and cobalt leaching from waste materials (e-waste, batteries, spent catalysts), aiming to provide a starting point for SOC recycling, not yet investigated. The literatu...
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description | Lanthanum and cobalt are Critical Raw Materials and components of Solid Oxide Cells—SOCs electrodes. This review analyses lanthanum and cobalt leaching from waste materials (e-waste, batteries, spent catalysts), aiming to provide a starting point for SOC recycling, not yet investigated. The literature was surveyed with a specific interest for leaching, the first phase of hydrometallurgy recycling. Most references (86%) were published after 2012, with an interest higher (85%) for cobalt. Inorganic acids were the prevailing (>80%) leaching agents, particularly for lanthanum, while leaching processes using organic acids mostly involved cobalt. The experimental conditions adopted more diluted organic acids (median 0.55 M for lanthanum and 1.4 M for cobalt) compared to inorganic acids (median value 2 M for both metals). Organic acids required a higher solid to liquid ratio (200 g/L), compared to inorganic ones (100 g/L) to solubilize lanthanum, while the opposite happened for cobalt (20 vs. 50 g/L). The process temperature didn’t change considerably with the solvent (45–75 °C for lanthanum, and 75–88 °C for cobalt). The contact time was higher for lanthanum than for cobalt (median 3–4 h vs. 75–85 min). Specific recycling processes are crucial to support SOCs value chain in Europe, and this review can help define the existing challenges and future perspectives. |
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This review analyses lanthanum and cobalt leaching from waste materials (e-waste, batteries, spent catalysts), aiming to provide a starting point for SOC recycling, not yet investigated. The literature was surveyed with a specific interest for leaching, the first phase of hydrometallurgy recycling. Most references (86%) were published after 2012, with an interest higher (85%) for cobalt. Inorganic acids were the prevailing (>80%) leaching agents, particularly for lanthanum, while leaching processes using organic acids mostly involved cobalt. The experimental conditions adopted more diluted organic acids (median 0.55 M for lanthanum and 1.4 M for cobalt) compared to inorganic acids (median value 2 M for both metals). Organic acids required a higher solid to liquid ratio (200 g/L), compared to inorganic ones (100 g/L) to solubilize lanthanum, while the opposite happened for cobalt (20 vs. 50 g/L). The process temperature didn’t change considerably with the solvent (45–75 °C for lanthanum, and 75–88 °C for cobalt). The contact time was higher for lanthanum than for cobalt (median 3–4 h vs. 75–85 min). Specific recycling processes are crucial to support SOCs value chain in Europe, and this review can help define the existing challenges and future perspectives.</description><identifier>ISSN: 2071-1050</identifier><identifier>EISSN: 2071-1050</identifier><identifier>DOI: 10.3390/su14063335</identifier><language>eng</language><publisher>Basel: MDPI AG</publisher><subject>Batteries ; Catalysts ; Catalytic cracking ; Classification ; Cobalt ; Efficiency ; Electrodes ; Electrolytes ; Electronic equipment and supplies ; Electronic waste ; Fuel cells ; Green chemistry ; Hydrometallurgy ; Inorganic acids ; Lanthanum ; Leaching ; Metals ; Organic acids ; Principles ; Raw materials ; Solvent extraction processes ; Value engineering ; Waste materials</subject><ispartof>Sustainability, 2022-03, Vol.14 (6), p.3335</ispartof><rights>COPYRIGHT 2022 MDPI AG</rights><rights>2022 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-c396t-bfdc09858b412ec19b66878766c64dab8d5671a4d2e27b7f3d68f878c1abe03f3</citedby><cites>FETCH-LOGICAL-c396t-bfdc09858b412ec19b66878766c64dab8d5671a4d2e27b7f3d68f878c1abe03f3</cites><orcidid>0000-0002-5015-8784 ; 0000-0001-5949-0559</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,776,780,27901,27902</link.rule.ids></links><search><creatorcontrib>Benedetto Mas, Alice</creatorcontrib><creatorcontrib>Fiore, Silvia</creatorcontrib><creatorcontrib>Fiorilli, Sonia</creatorcontrib><creatorcontrib>Smeacetto, Federico</creatorcontrib><creatorcontrib>Santarelli, Massimo</creatorcontrib><creatorcontrib>Schiavi, Ilaria</creatorcontrib><title>Analysis of Lanthanum and Cobalt Leaching Aimed at Effective Recycling Strategies of Solid Oxide Cells</title><title>Sustainability</title><description>Lanthanum and cobalt are Critical Raw Materials and components of Solid Oxide Cells—SOCs electrodes. This review analyses lanthanum and cobalt leaching from waste materials (e-waste, batteries, spent catalysts), aiming to provide a starting point for SOC recycling, not yet investigated. The literature was surveyed with a specific interest for leaching, the first phase of hydrometallurgy recycling. Most references (86%) were published after 2012, with an interest higher (85%) for cobalt. Inorganic acids were the prevailing (>80%) leaching agents, particularly for lanthanum, while leaching processes using organic acids mostly involved cobalt. The experimental conditions adopted more diluted organic acids (median 0.55 M for lanthanum and 1.4 M for cobalt) compared to inorganic acids (median value 2 M for both metals). Organic acids required a higher solid to liquid ratio (200 g/L), compared to inorganic ones (100 g/L) to solubilize lanthanum, while the opposite happened for cobalt (20 vs. 50 g/L). The process temperature didn’t change considerably with the solvent (45–75 °C for lanthanum, and 75–88 °C for cobalt). The contact time was higher for lanthanum than for cobalt (median 3–4 h vs. 75–85 min). Specific recycling processes are crucial to support SOCs value chain in Europe, and this review can help define the existing challenges and future perspectives.</description><subject>Batteries</subject><subject>Catalysts</subject><subject>Catalytic cracking</subject><subject>Classification</subject><subject>Cobalt</subject><subject>Efficiency</subject><subject>Electrodes</subject><subject>Electrolytes</subject><subject>Electronic equipment and supplies</subject><subject>Electronic waste</subject><subject>Fuel cells</subject><subject>Green chemistry</subject><subject>Hydrometallurgy</subject><subject>Inorganic acids</subject><subject>Lanthanum</subject><subject>Leaching</subject><subject>Metals</subject><subject>Organic acids</subject><subject>Principles</subject><subject>Raw materials</subject><subject>Solvent extraction processes</subject><subject>Value engineering</subject><subject>Waste materials</subject><issn>2071-1050</issn><issn>2071-1050</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2022</creationdate><recordtype>article</recordtype><sourceid>BENPR</sourceid><recordid>eNptkU1rwzAMhsPYYKXrZb_AsNMG7fyROMmxlG4rBArtdjaOLacu-ehiZ7T_fuk66AqTDhLS8woJBcE9wRPGUvzsOhJizhiLroIBxTEZExzh6z_5bTBybot7Y4ykhA8CM61leXDWocagTNZ-I-uuQrLWaNbksvQoA6k2ti7Q1FagkfRobgwob78ArUAdVHlsrn0rPRQWfgatm9JqtNxbDWgGZenughsjSwej3zgMPl7m77O3cbZ8Xcym2VixlPtxbrTCaRIleUgoKJLmnCdxEnOueKhlnuiIx0SGmgKN89gwzRPTA4rIHDAzbBg8nObu2uazA-fFtuna_kQnKA8p51FMwzNVyBKErU3Tb68q65SYJhRzGmEe9dTkH6p3DZVVTQ3G9vULweOFoGc87H0hO-fEYr26ZJ9OrGob51owYtfaSrYHQbA4flOcv8m-AXBejpA</recordid><startdate>20220301</startdate><enddate>20220301</enddate><creator>Benedetto Mas, Alice</creator><creator>Fiore, Silvia</creator><creator>Fiorilli, Sonia</creator><creator>Smeacetto, Federico</creator><creator>Santarelli, Massimo</creator><creator>Schiavi, Ilaria</creator><general>MDPI AG</general><scope>AAYXX</scope><scope>CITATION</scope><scope>ISR</scope><scope>4U-</scope><scope>ABUWG</scope><scope>AFKRA</scope><scope>AZQEC</scope><scope>BENPR</scope><scope>CCPQU</scope><scope>DWQXO</scope><scope>PIMPY</scope><scope>PQEST</scope><scope>PQQKQ</scope><scope>PQUKI</scope><orcidid>https://orcid.org/0000-0002-5015-8784</orcidid><orcidid>https://orcid.org/0000-0001-5949-0559</orcidid></search><sort><creationdate>20220301</creationdate><title>Analysis of Lanthanum and Cobalt Leaching Aimed at Effective Recycling Strategies of Solid Oxide Cells</title><author>Benedetto Mas, Alice ; 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This review analyses lanthanum and cobalt leaching from waste materials (e-waste, batteries, spent catalysts), aiming to provide a starting point for SOC recycling, not yet investigated. The literature was surveyed with a specific interest for leaching, the first phase of hydrometallurgy recycling. Most references (86%) were published after 2012, with an interest higher (85%) for cobalt. Inorganic acids were the prevailing (>80%) leaching agents, particularly for lanthanum, while leaching processes using organic acids mostly involved cobalt. The experimental conditions adopted more diluted organic acids (median 0.55 M for lanthanum and 1.4 M for cobalt) compared to inorganic acids (median value 2 M for both metals). Organic acids required a higher solid to liquid ratio (200 g/L), compared to inorganic ones (100 g/L) to solubilize lanthanum, while the opposite happened for cobalt (20 vs. 50 g/L). The process temperature didn’t change considerably with the solvent (45–75 °C for lanthanum, and 75–88 °C for cobalt). The contact time was higher for lanthanum than for cobalt (median 3–4 h vs. 75–85 min). Specific recycling processes are crucial to support SOCs value chain in Europe, and this review can help define the existing challenges and future perspectives.</abstract><cop>Basel</cop><pub>MDPI AG</pub><doi>10.3390/su14063335</doi><orcidid>https://orcid.org/0000-0002-5015-8784</orcidid><orcidid>https://orcid.org/0000-0001-5949-0559</orcidid><oa>free_for_read</oa></addata></record> |
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subjects | Batteries Catalysts Catalytic cracking Classification Cobalt Efficiency Electrodes Electrolytes Electronic equipment and supplies Electronic waste Fuel cells Green chemistry Hydrometallurgy Inorganic acids Lanthanum Leaching Metals Organic acids Principles Raw materials Solvent extraction processes Value engineering Waste materials |
title | Analysis of Lanthanum and Cobalt Leaching Aimed at Effective Recycling Strategies of Solid Oxide Cells |
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