Selective extraction of vanadium from chromium by pure [C8mim][PF6]: An anion exchange process

[Display omitted] •The maximum βV/Cr by pure [C8mim][PF6] was 100.6 in case of pH 3.5.•The extraction mechanism could be the anion exchange between HV10O273− and PF6−.•A novel approach to prepare ionic liquids with metal oxo-anions as counter anion.•Vanadate-loaded IL phase can be quantitatively str...

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Veröffentlicht in:Separation and purification technology 2014-06, Vol.131, p.94-101
Hauptverfasser: Hu, Qiaoyu, Zhao, Junmei, Wang, Fuchun, Huo, Fang, Liu, Huizhou
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Zhao, Junmei
Wang, Fuchun
Huo, Fang
Liu, Huizhou
description [Display omitted] •The maximum βV/Cr by pure [C8mim][PF6] was 100.6 in case of pH 3.5.•The extraction mechanism could be the anion exchange between HV10O273− and PF6−.•A novel approach to prepare ionic liquids with metal oxo-anions as counter anion.•Vanadate-loaded IL phase can be quantitatively stripped by KPF6 and NaOH.•Pure [C8mim][PF6] could be used to recover V(V) from Cr(VI)-containing solutions. Separations among vanadium(V) and chromium(VI) remain challenging. The extraction behaviors of V(V) along with Cr(VI) by a few of pure imidazolium-based hydrophobic ionic liquids have been investigated. Among these hydrophobic ionic liquids, [C8mim][PF6] exhibits a special extraction for V(V) while a weak extraction for Cr(VI). The extraction behavior of V(V) by [C8mim][PF6] was particularly studied. The extraction of V(V) is strongly dependent on the acidity of the aqueous phase, and the maximum separation factor between V and Cr (βV/Cr) was calculated to be 100.6 in case of pH 3.5. The most probable extraction mechanism of V(V) has been proposed to be the anion exchange between the main species HV10O273− and PF6−. Furthermore, V(V) in IL phase can be quantitatively stripped by KPF6 solution under the basic condition (COH−=1mol/l). Recycle test indicates that the extraction capacity shows no apparent decline until the 9th continuous extraction–stripping cycle. The result also provides a new approach for the preparation of a novel ionic liquid with metal oxo-anions as counter anion.
doi_str_mv 10.1016/j.seppur.2014.05.003
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Separations among vanadium(V) and chromium(VI) remain challenging. The extraction behaviors of V(V) along with Cr(VI) by a few of pure imidazolium-based hydrophobic ionic liquids have been investigated. Among these hydrophobic ionic liquids, [C8mim][PF6] exhibits a special extraction for V(V) while a weak extraction for Cr(VI). The extraction behavior of V(V) by [C8mim][PF6] was particularly studied. The extraction of V(V) is strongly dependent on the acidity of the aqueous phase, and the maximum separation factor between V and Cr (βV/Cr) was calculated to be 100.6 in case of pH 3.5. The most probable extraction mechanism of V(V) has been proposed to be the anion exchange between the main species HV10O273− and PF6−. Furthermore, V(V) in IL phase can be quantitatively stripped by KPF6 solution under the basic condition (COH−=1mol/l). Recycle test indicates that the extraction capacity shows no apparent decline until the 9th continuous extraction–stripping cycle. The result also provides a new approach for the preparation of a novel ionic liquid with metal oxo-anions as counter anion.</description><identifier>ISSN: 1383-5866</identifier><identifier>EISSN: 1873-3794</identifier><identifier>DOI: 10.1016/j.seppur.2014.05.003</identifier><language>eng</language><publisher>Elsevier B.V</publisher><subject>[C8mim][PF6] ; Anion exchanging ; Chromium ; Chromium(IV) ; Exchange ; Extraction ; Ionic liquids ; Mathematical analysis ; Purification ; Separation ; Vanadium(V)</subject><ispartof>Separation and purification technology, 2014-06, Vol.131, p.94-101</ispartof><rights>2014 Elsevier B.V.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c376t-a5eb3cbe7c599b73ab2381d7930a8df82e16eaa1c7604ccbf80f9e9229f78ea13</citedby><cites>FETCH-LOGICAL-c376t-a5eb3cbe7c599b73ab2381d7930a8df82e16eaa1c7604ccbf80f9e9229f78ea13</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.seppur.2014.05.003$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3550,27924,27925,45995</link.rule.ids></links><search><creatorcontrib>Hu, Qiaoyu</creatorcontrib><creatorcontrib>Zhao, Junmei</creatorcontrib><creatorcontrib>Wang, Fuchun</creatorcontrib><creatorcontrib>Huo, Fang</creatorcontrib><creatorcontrib>Liu, Huizhou</creatorcontrib><title>Selective extraction of vanadium from chromium by pure [C8mim][PF6]: An anion exchange process</title><title>Separation and purification technology</title><description>[Display omitted] •The maximum βV/Cr by pure [C8mim][PF6] was 100.6 in case of pH 3.5.•The extraction mechanism could be the anion exchange between HV10O273− and PF6−.•A novel approach to prepare ionic liquids with metal oxo-anions as counter anion.•Vanadate-loaded IL phase can be quantitatively stripped by KPF6 and NaOH.•Pure [C8mim][PF6] could be used to recover V(V) from Cr(VI)-containing solutions. Separations among vanadium(V) and chromium(VI) remain challenging. The extraction behaviors of V(V) along with Cr(VI) by a few of pure imidazolium-based hydrophobic ionic liquids have been investigated. Among these hydrophobic ionic liquids, [C8mim][PF6] exhibits a special extraction for V(V) while a weak extraction for Cr(VI). The extraction behavior of V(V) by [C8mim][PF6] was particularly studied. The extraction of V(V) is strongly dependent on the acidity of the aqueous phase, and the maximum separation factor between V and Cr (βV/Cr) was calculated to be 100.6 in case of pH 3.5. The most probable extraction mechanism of V(V) has been proposed to be the anion exchange between the main species HV10O273− and PF6−. Furthermore, V(V) in IL phase can be quantitatively stripped by KPF6 solution under the basic condition (COH−=1mol/l). Recycle test indicates that the extraction capacity shows no apparent decline until the 9th continuous extraction–stripping cycle. 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Separations among vanadium(V) and chromium(VI) remain challenging. The extraction behaviors of V(V) along with Cr(VI) by a few of pure imidazolium-based hydrophobic ionic liquids have been investigated. Among these hydrophobic ionic liquids, [C8mim][PF6] exhibits a special extraction for V(V) while a weak extraction for Cr(VI). The extraction behavior of V(V) by [C8mim][PF6] was particularly studied. The extraction of V(V) is strongly dependent on the acidity of the aqueous phase, and the maximum separation factor between V and Cr (βV/Cr) was calculated to be 100.6 in case of pH 3.5. The most probable extraction mechanism of V(V) has been proposed to be the anion exchange between the main species HV10O273− and PF6−. Furthermore, V(V) in IL phase can be quantitatively stripped by KPF6 solution under the basic condition (COH−=1mol/l). Recycle test indicates that the extraction capacity shows no apparent decline until the 9th continuous extraction–stripping cycle. 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source ScienceDirect Journals (5 years ago - present)
subjects [C8mim][PF6]
Anion exchanging
Chromium
Chromium(IV)
Exchange
Extraction
Ionic liquids
Mathematical analysis
Purification
Separation
Vanadium(V)
title Selective extraction of vanadium from chromium by pure [C8mim][PF6]: An anion exchange process
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