Investigation of the extraction of samarium and gadolinium from leaching solutions of phosphorus-containing raw materials using solid extractants
AbstractIn accordance with the State Program of the Russian Federation «Development of Industry and Its Competitiveness», as well as the absence of balance deposits of rare earth metals on the territory of the Russian Federation, it is urgent to study methods for the extraction and separation of rar...
Ausführliche Beschreibung
Autor*in: |
Denis Sergeevich Lutskiy [verfasserIn] Elena Sergeevna Lukyantseva [verfasserIn] Valeria Yurievna Mikheeva [verfasserIn] Lyudmila Vladislavovna Grigorieva [verfasserIn] |
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E-Artikel |
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Sprache: |
Englisch |
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2023 |
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In: Arab Journal of Basic and Applied Sciences - Taylor & Francis Group, 2018, 30(2023), 1, Seite 68-73 |
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Übergeordnetes Werk: |
volume:30 ; year:2023 ; number:1 ; pages:68-73 |
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DOI / URN: |
10.1080/25765299.2022.2157954 |
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Katalog-ID: |
DOAJ08846945X |
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10.1080/25765299.2022.2157954 doi (DE-627)DOAJ08846945X (DE-599)DOAJ7c686f0ab4d540d2ace7c53b605d12e8 DE-627 ger DE-627 rakwb eng Denis Sergeevich Lutskiy verfasserin aut Investigation of the extraction of samarium and gadolinium from leaching solutions of phosphorus-containing raw materials using solid extractants 2023 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier AbstractIn accordance with the State Program of the Russian Federation «Development of Industry and Its Competitiveness», as well as the absence of balance deposits of rare earth metals on the territory of the Russian Federation, it is urgent to study methods for the extraction and separation of rare earth metals from technological solutions obtained during the processing of apatite concentrates. The article is devoted to the study of the kinetic features of solid-phase extraction of samarium (III) and gadolinium (III) from simulated industrial phosphoric acid solutions. Levextrel resine (co-polymerization product of styrene and divinylbenzene) containing Di-2-ethylhexylphosphoric acid (D2EHPA) – was used as a solid-phase extraction agent. Significant dependence of samarium (III) and gadolinium (III) extraction rate constant on the stirring rate was revealed using the formal first-order kinetic equation. Based on the linear dependences of the logarithm of the reaction rate constant on the reciprocal temperature, the activation energies for the extraction of Gd and Sm from phosphate model solutions were established, which, respectively, were 42.47 and 28.48 kJ/mol. The obtained values of the activation energies indicate that the limiting stage of the extraction process on a solid extractant can be considered a chemical reaction between ions of rare-earth metals and functional groups of the extractant. Separation of elements at the extraction stage is possible at temperature of 333 K under non-equilibrium conditions with separation coefficient up to 1.8 in 5 min. Apatite concentrate extraction rare earth metals SES SES-D2EHPA solid extractant system Science Q Elena Sergeevna Lukyantseva verfasserin aut Valeria Yurievna Mikheeva verfasserin aut Lyudmila Vladislavovna Grigorieva verfasserin aut In Arab Journal of Basic and Applied Sciences Taylor & Francis Group, 2018 30(2023), 1, Seite 68-73 (DE-627)1679235850 25765299 nnns volume:30 year:2023 number:1 pages:68-73 https://doi.org/10.1080/25765299.2022.2157954 kostenfrei https://doaj.org/article/7c686f0ab4d540d2ace7c53b605d12e8 kostenfrei https://www.tandfonline.com/doi/10.1080/25765299.2022.2157954 kostenfrei https://doaj.org/toc/2576-5299 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_95 GBV_ILN_105 GBV_ILN_110 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_213 GBV_ILN_230 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_2014 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 30 2023 1 68-73 |
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Denis Sergeevich Lutskiy misc Apatite concentrate misc extraction misc rare earth metals misc SES misc SES-D2EHPA misc solid extractant system misc Science misc Q Investigation of the extraction of samarium and gadolinium from leaching solutions of phosphorus-containing raw materials using solid extractants |
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Investigation of the extraction of samarium and gadolinium from leaching solutions of phosphorus-containing raw materials using solid extractants Apatite concentrate extraction rare earth metals SES SES-D2EHPA solid extractant system |
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investigation of the extraction of samarium and gadolinium from leaching solutions of phosphorus-containing raw materials using solid extractants |
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Investigation of the extraction of samarium and gadolinium from leaching solutions of phosphorus-containing raw materials using solid extractants |
abstract |
AbstractIn accordance with the State Program of the Russian Federation «Development of Industry and Its Competitiveness», as well as the absence of balance deposits of rare earth metals on the territory of the Russian Federation, it is urgent to study methods for the extraction and separation of rare earth metals from technological solutions obtained during the processing of apatite concentrates. The article is devoted to the study of the kinetic features of solid-phase extraction of samarium (III) and gadolinium (III) from simulated industrial phosphoric acid solutions. Levextrel resine (co-polymerization product of styrene and divinylbenzene) containing Di-2-ethylhexylphosphoric acid (D2EHPA) – was used as a solid-phase extraction agent. Significant dependence of samarium (III) and gadolinium (III) extraction rate constant on the stirring rate was revealed using the formal first-order kinetic equation. Based on the linear dependences of the logarithm of the reaction rate constant on the reciprocal temperature, the activation energies for the extraction of Gd and Sm from phosphate model solutions were established, which, respectively, were 42.47 and 28.48 kJ/mol. The obtained values of the activation energies indicate that the limiting stage of the extraction process on a solid extractant can be considered a chemical reaction between ions of rare-earth metals and functional groups of the extractant. Separation of elements at the extraction stage is possible at temperature of 333 K under non-equilibrium conditions with separation coefficient up to 1.8 in 5 min. |
abstractGer |
AbstractIn accordance with the State Program of the Russian Federation «Development of Industry and Its Competitiveness», as well as the absence of balance deposits of rare earth metals on the territory of the Russian Federation, it is urgent to study methods for the extraction and separation of rare earth metals from technological solutions obtained during the processing of apatite concentrates. The article is devoted to the study of the kinetic features of solid-phase extraction of samarium (III) and gadolinium (III) from simulated industrial phosphoric acid solutions. Levextrel resine (co-polymerization product of styrene and divinylbenzene) containing Di-2-ethylhexylphosphoric acid (D2EHPA) – was used as a solid-phase extraction agent. Significant dependence of samarium (III) and gadolinium (III) extraction rate constant on the stirring rate was revealed using the formal first-order kinetic equation. Based on the linear dependences of the logarithm of the reaction rate constant on the reciprocal temperature, the activation energies for the extraction of Gd and Sm from phosphate model solutions were established, which, respectively, were 42.47 and 28.48 kJ/mol. The obtained values of the activation energies indicate that the limiting stage of the extraction process on a solid extractant can be considered a chemical reaction between ions of rare-earth metals and functional groups of the extractant. Separation of elements at the extraction stage is possible at temperature of 333 K under non-equilibrium conditions with separation coefficient up to 1.8 in 5 min. |
abstract_unstemmed |
AbstractIn accordance with the State Program of the Russian Federation «Development of Industry and Its Competitiveness», as well as the absence of balance deposits of rare earth metals on the territory of the Russian Federation, it is urgent to study methods for the extraction and separation of rare earth metals from technological solutions obtained during the processing of apatite concentrates. The article is devoted to the study of the kinetic features of solid-phase extraction of samarium (III) and gadolinium (III) from simulated industrial phosphoric acid solutions. Levextrel resine (co-polymerization product of styrene and divinylbenzene) containing Di-2-ethylhexylphosphoric acid (D2EHPA) – was used as a solid-phase extraction agent. Significant dependence of samarium (III) and gadolinium (III) extraction rate constant on the stirring rate was revealed using the formal first-order kinetic equation. Based on the linear dependences of the logarithm of the reaction rate constant on the reciprocal temperature, the activation energies for the extraction of Gd and Sm from phosphate model solutions were established, which, respectively, were 42.47 and 28.48 kJ/mol. The obtained values of the activation energies indicate that the limiting stage of the extraction process on a solid extractant can be considered a chemical reaction between ions of rare-earth metals and functional groups of the extractant. Separation of elements at the extraction stage is possible at temperature of 333 K under non-equilibrium conditions with separation coefficient up to 1.8 in 5 min. |
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Investigation of the extraction of samarium and gadolinium from leaching solutions of phosphorus-containing raw materials using solid extractants |
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The obtained values of the activation energies indicate that the limiting stage of the extraction process on a solid extractant can be considered a chemical reaction between ions of rare-earth metals and functional groups of the extractant. 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Lukyantseva</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="0" ind2=" "><subfield code="a">Valeria Yurievna Mikheeva</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="0" ind2=" "><subfield code="a">Lyudmila Vladislavovna Grigorieva</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">In</subfield><subfield code="t">Arab Journal of Basic and Applied Sciences</subfield><subfield code="d">Taylor & Francis Group, 2018</subfield><subfield code="g">30(2023), 1, Seite 68-73</subfield><subfield code="w">(DE-627)1679235850</subfield><subfield code="x">25765299</subfield><subfield code="7">nnns</subfield></datafield><datafield tag="773" ind1="1" ind2="8"><subfield code="g">volume:30</subfield><subfield code="g">year:2023</subfield><subfield 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