Näytä suppeat kuvailutiedot

dc.contributor.authorPerämäki, Siiri
dc.contributor.authorTiihonen, Antti
dc.contributor.authorRajahalme, Joona
dc.contributor.authorLarsson, Sylva
dc.contributor.authorLahtinen, Elmeri
dc.contributor.authorNiskanen, Joni
dc.contributor.authorBudhathoki, Roshan
dc.contributor.authorVäisänen, Ari
dc.date.accessioned2022-08-17T10:09:36Z
dc.date.available2022-08-17T10:09:36Z
dc.date.issued2022
dc.identifier.citationPerämäki, S., Tiihonen, A., Rajahalme, J., Larsson, S., Lahtinen, E., Niskanen, J., Budhathoki, R., & Väisänen, A. (2022). Dry chlorination of spent nickel metal hydride battery waste for water leaching of battery metals and rare earth elements. <i>Journal of Environmental Chemical Engineering</i>, <i>10</i>(5), Article 108200. <a href="https://doi.org/10.1016/j.jece.2022.108200" target="_blank">https://doi.org/10.1016/j.jece.2022.108200</a>
dc.identifier.otherCONVID_148880947
dc.identifier.urihttps://jyx.jyu.fi/handle/123456789/82653
dc.description.abstractAn efficient leaching process was developed for nickel, cobalt, and the rare earth elements (REEs) from spent nickel metal hydride (NiMH) battery waste. The process involves dry chlorination with ammonium chloride in low temperature to produce water-soluble chlorinated compounds, followed by simple water leaching. The factors affecting the conversion and solubilization were studied, including the amount of ammonium chloride, residence time and temperature in dry chlorination, and solid to liquid ratio, time and temperature in water leaching. As a result, the dry chlorination process was found to produce ammonium and chloride containing products, depending on the temperature of the process: ammonium metal chlorides were produced in temperatures of 250-300 ℃, while increasing the temperature to 350 ℃ resulted in formation of metal chlorides. Overall, highest metal recoveries were achieved during 60 min residence time at a temperature of 350 °C, where ammonium is no longer present and ammonium metal chlorides and metal chlorides have formed. Water leaching was found to proceed rapidly, especially for REEs, and yields of 87% for Ni, 98% for Co, 94% for Ce, and 96% for La were attained during 60 min of leaching in room temperature. This study introduces a process, which is considered as an environmentally more benign alternative to traditional mineral acid leaching, resulting in high metal leaching efficiencies with neutral leachates, requiring no chemical-intensive neutralization steps in the following processing.en
dc.format.mimetypeapplication/pdf
dc.language.isoeng
dc.publisherElsevier
dc.relation.ispartofseriesJournal of Environmental Chemical Engineering
dc.rightsCC BY 4.0
dc.subject.otherNiMH
dc.subject.otherbattery
dc.subject.otherdry chlorination
dc.titleDry chlorination of spent nickel metal hydride battery waste for water leaching of battery metals and rare earth elements
dc.typeresearch article
dc.identifier.urnURN:NBN:fi:jyu-202208174196
dc.contributor.laitosKemian laitosfi
dc.contributor.laitosDepartment of Chemistryen
dc.contributor.oppiaineEpäorgaaninen ja analyyttinen kemiafi
dc.contributor.oppiaineAnalyyttinen kemiafi
dc.contributor.oppiaineResurssiviisausyhteisöfi
dc.contributor.oppiaineSoveltava kemiafi
dc.contributor.oppiaineEpäorgaaninen kemiafi
dc.contributor.oppiaineOrgaaninen kemiafi
dc.contributor.oppiaineInorganic and Analytical Chemistryen
dc.contributor.oppiaineAnalytical Chemistryen
dc.contributor.oppiaineSchool of Resource Wisdomen
dc.contributor.oppiaineApplied Chemistryen
dc.contributor.oppiaineInorganic Chemistryen
dc.contributor.oppiaineOrganic Chemistryen
dc.type.urihttp://purl.org/eprint/type/JournalArticle
dc.type.coarhttp://purl.org/coar/resource_type/c_2df8fbb1
dc.description.reviewstatuspeerReviewed
dc.relation.issn2213-3437
dc.relation.numberinseries5
dc.relation.volume10
dc.type.versionpublishedVersion
dc.rights.copyright© 2022 The Authors. Published by Elsevier Ltd.
dc.rights.accesslevelopenAccessfi
dc.type.publicationarticle
dc.relation.grantnumberA74540
dc.subject.ysoharvinaiset maametallit
dc.subject.ysonikkelimetallihydridiakut
dc.subject.ysoakut
dc.subject.ysojätteiden hyötykäyttö
dc.subject.ysoprosessit
dc.subject.ysoliuotus
dc.subject.ysoympäristöystävällisyys
dc.subject.ysonikkeli
dc.subject.ysokoboltti
dc.subject.ysokloridit
dc.format.contentfulltext
jyx.subject.urihttp://www.yso.fi/onto/yso/p15798
jyx.subject.urihttp://www.yso.fi/onto/yso/p39428
jyx.subject.urihttp://www.yso.fi/onto/yso/p2306
jyx.subject.urihttp://www.yso.fi/onto/yso/p2180
jyx.subject.urihttp://www.yso.fi/onto/yso/p2111
jyx.subject.urihttp://www.yso.fi/onto/yso/p9032
jyx.subject.urihttp://www.yso.fi/onto/yso/p23825
jyx.subject.urihttp://www.yso.fi/onto/yso/p19926
jyx.subject.urihttp://www.yso.fi/onto/yso/p15221
jyx.subject.urihttp://www.yso.fi/onto/yso/p12355
dc.rights.urlhttps://creativecommons.org/licenses/by/4.0/
dc.relation.doi10.1016/j.jece.2022.108200
dc.relation.funderCouncil of Tampere Regionen
dc.relation.funderPirkanmaan liittofi
jyx.fundingprogramERDF European Regional Development Fund, React-EUen
jyx.fundingprogramEAKR Euroopan aluekehitysrahasto, React-EUfi
jyx.fundinginformationThis work was supported by the European Regional Development Fund (grant number: A74540) and the Department of Chemistry at University of Jyväskylä.
dc.type.okmA1


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