Application of aqueous two-phase systems for the development of a new method of cobalt(II), iron(III) and nickel(II) extraction: A green chemistry approach
Autor(a) principal: | |
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Data de Publicação: | 2011 |
Outros Autores: | , , |
Tipo de documento: | Artigo |
Idioma: | eng |
Título da fonte: | LOCUS Repositório Institucional da UFV |
Texto Completo: | https://doi.org/10.1016/j.jhazmat.2011.07.062 http://www.locus.ufv.br/handle/123456789/13277 |
Resumo: | We have investigated the extraction behavior of the metallic ions Co(II), Fe(III) and Ni(II) as a function of the amount of potassium thiocyanate used as an extracting agent, using the following aque-ous two-phase systems (ATPS): PEO + (NH 4 ) 2 SO 4 + H 2 O, PEO + Li 2 SO 4 + H 2 O, L35 + (NH 4 ) 2 SO 4 + H 2 O and L35 + (Li) 2 SO 4 + H 2 O. Metal extraction from the salt-rich phase to the polymer-rich phase is affected by the following parameters: amount of added extractant, pH, and the nature of the electrolyte and polymer that forms the ATPS. Maximal extraction percentages were obtained for Co(II) (99.8%), Fe(III) (12.7%) and Ni(II) (3.17%) when the ATPS was composed of PEO1500 + (NH 4 ) 2 SO 4 + H 2 O containing 1.4 mmol of KSCN at pH 4.0, providing separation factors as high as S Co,Fe = 3440 and S Co,Ni = 15,300. However, when the same ATPS was used at pH 2.0, the maximal extraction percentages for iron and nickel were 99.5% and 4.34%, respectively, with S Fe,Ni equal to 4380. The proposed technique was shown to be efficient in the extraction of Co(II) and Fe(III), with large viability for the selective separation of Co(II) and Fe(III) ions in the presence of Ni(II). |
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Patrício, Pamela da RochaMesquita, Maiby CabralSilva, Luis Henrique Mendes daSilva, Maria C. Hespanhol da2017-11-20T10:14:57Z2017-11-20T10:14:57Z2011-10-150304-3894https://doi.org/10.1016/j.jhazmat.2011.07.062http://www.locus.ufv.br/handle/123456789/13277We have investigated the extraction behavior of the metallic ions Co(II), Fe(III) and Ni(II) as a function of the amount of potassium thiocyanate used as an extracting agent, using the following aque-ous two-phase systems (ATPS): PEO + (NH 4 ) 2 SO 4 + H 2 O, PEO + Li 2 SO 4 + H 2 O, L35 + (NH 4 ) 2 SO 4 + H 2 O and L35 + (Li) 2 SO 4 + H 2 O. Metal extraction from the salt-rich phase to the polymer-rich phase is affected by the following parameters: amount of added extractant, pH, and the nature of the electrolyte and polymer that forms the ATPS. Maximal extraction percentages were obtained for Co(II) (99.8%), Fe(III) (12.7%) and Ni(II) (3.17%) when the ATPS was composed of PEO1500 + (NH 4 ) 2 SO 4 + H 2 O containing 1.4 mmol of KSCN at pH 4.0, providing separation factors as high as S Co,Fe = 3440 and S Co,Ni = 15,300. However, when the same ATPS was used at pH 2.0, the maximal extraction percentages for iron and nickel were 99.5% and 4.34%, respectively, with S Fe,Ni equal to 4380. The proposed technique was shown to be efficient in the extraction of Co(II) and Fe(III), with large viability for the selective separation of Co(II) and Fe(III) ions in the presence of Ni(II).engJournal of Hazardous MaterialsVolume 193, Pages 311-318, October 2011Aqueous two-phase systemsLiquid–liquid extraction without organicSolventCobaltIronNickelApplication of aqueous two-phase systems for the development of a new method of cobalt(II), iron(III) and nickel(II) extraction: A green chemistry approachinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleapplication/pdfinfo:eu-repo/semantics/openAccessreponame:LOCUS Repositório Institucional da UFVinstname:Universidade Federal de Viçosa (UFV)instacron:UFVORIGINAL1-s2.0-S0304389411009435-main.pdf1-s2.0-S0304389411009435-main.pdftexto completoapplication/pdf395461https://locus.ufv.br//bitstream/123456789/13277/1/1-s2.0-S0304389411009435-main.pdff4fa4bcbfaba84fdeab6d1f89c6bc22dMD51LICENSElicense.txtlicense.txttext/plain; charset=utf-81748https://locus.ufv.br//bitstream/123456789/13277/2/license.txt8a4605be74aa9ea9d79846c1fba20a33MD52THUMBNAIL1-s2.0-S0304389411009435-main.pdf.jpg1-s2.0-S0304389411009435-main.pdf.jpgIM Thumbnailimage/jpeg5212https://locus.ufv.br//bitstream/123456789/13277/3/1-s2.0-S0304389411009435-main.pdf.jpg315d360a533418e95b812f8c64ef2024MD53123456789/132772017-11-20 22:00:37.151oai:locus.ufv.br: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Repositório InstitucionalPUBhttps://www.locus.ufv.br/oai/requestfabiojreis@ufv.bropendoar:21452017-11-21T01:00:37LOCUS Repositório Institucional da UFV - Universidade Federal de Viçosa (UFV)false |
dc.title.en.fl_str_mv |
Application of aqueous two-phase systems for the development of a new method of cobalt(II), iron(III) and nickel(II) extraction: A green chemistry approach |
title |
Application of aqueous two-phase systems for the development of a new method of cobalt(II), iron(III) and nickel(II) extraction: A green chemistry approach |
spellingShingle |
Application of aqueous two-phase systems for the development of a new method of cobalt(II), iron(III) and nickel(II) extraction: A green chemistry approach Patrício, Pamela da Rocha Aqueous two-phase systems Liquid–liquid extraction without organic Solvent Cobalt Iron Nickel |
title_short |
Application of aqueous two-phase systems for the development of a new method of cobalt(II), iron(III) and nickel(II) extraction: A green chemistry approach |
title_full |
Application of aqueous two-phase systems for the development of a new method of cobalt(II), iron(III) and nickel(II) extraction: A green chemistry approach |
title_fullStr |
Application of aqueous two-phase systems for the development of a new method of cobalt(II), iron(III) and nickel(II) extraction: A green chemistry approach |
title_full_unstemmed |
Application of aqueous two-phase systems for the development of a new method of cobalt(II), iron(III) and nickel(II) extraction: A green chemistry approach |
title_sort |
Application of aqueous two-phase systems for the development of a new method of cobalt(II), iron(III) and nickel(II) extraction: A green chemistry approach |
author |
Patrício, Pamela da Rocha |
author_facet |
Patrício, Pamela da Rocha Mesquita, Maiby Cabral Silva, Luis Henrique Mendes da Silva, Maria C. Hespanhol da |
author_role |
author |
author2 |
Mesquita, Maiby Cabral Silva, Luis Henrique Mendes da Silva, Maria C. Hespanhol da |
author2_role |
author author author |
dc.contributor.author.fl_str_mv |
Patrício, Pamela da Rocha Mesquita, Maiby Cabral Silva, Luis Henrique Mendes da Silva, Maria C. Hespanhol da |
dc.subject.pt-BR.fl_str_mv |
Aqueous two-phase systems Liquid–liquid extraction without organic Solvent Cobalt Iron Nickel |
topic |
Aqueous two-phase systems Liquid–liquid extraction without organic Solvent Cobalt Iron Nickel |
description |
We have investigated the extraction behavior of the metallic ions Co(II), Fe(III) and Ni(II) as a function of the amount of potassium thiocyanate used as an extracting agent, using the following aque-ous two-phase systems (ATPS): PEO + (NH 4 ) 2 SO 4 + H 2 O, PEO + Li 2 SO 4 + H 2 O, L35 + (NH 4 ) 2 SO 4 + H 2 O and L35 + (Li) 2 SO 4 + H 2 O. Metal extraction from the salt-rich phase to the polymer-rich phase is affected by the following parameters: amount of added extractant, pH, and the nature of the electrolyte and polymer that forms the ATPS. Maximal extraction percentages were obtained for Co(II) (99.8%), Fe(III) (12.7%) and Ni(II) (3.17%) when the ATPS was composed of PEO1500 + (NH 4 ) 2 SO 4 + H 2 O containing 1.4 mmol of KSCN at pH 4.0, providing separation factors as high as S Co,Fe = 3440 and S Co,Ni = 15,300. However, when the same ATPS was used at pH 2.0, the maximal extraction percentages for iron and nickel were 99.5% and 4.34%, respectively, with S Fe,Ni equal to 4380. The proposed technique was shown to be efficient in the extraction of Co(II) and Fe(III), with large viability for the selective separation of Co(II) and Fe(III) ions in the presence of Ni(II). |
publishDate |
2011 |
dc.date.issued.fl_str_mv |
2011-10-15 |
dc.date.accessioned.fl_str_mv |
2017-11-20T10:14:57Z |
dc.date.available.fl_str_mv |
2017-11-20T10:14:57Z |
dc.type.status.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/article |
format |
article |
status_str |
publishedVersion |
dc.identifier.uri.fl_str_mv |
https://doi.org/10.1016/j.jhazmat.2011.07.062 http://www.locus.ufv.br/handle/123456789/13277 |
dc.identifier.issn.none.fl_str_mv |
0304-3894 |
identifier_str_mv |
0304-3894 |
url |
https://doi.org/10.1016/j.jhazmat.2011.07.062 http://www.locus.ufv.br/handle/123456789/13277 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.ispartofseries.pt-BR.fl_str_mv |
Volume 193, Pages 311-318, October 2011 |
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openAccess |
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Journal of Hazardous Materials |
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Journal of Hazardous Materials |
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