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dc.contributor.authorShoppert, A.en
dc.contributor.authorLoginova, I.en
dc.contributor.authorNapol’skikh, J.en
dc.contributor.authorKyrchikov, A.en
dc.contributor.authorChaikin, L.en
dc.contributor.authorRogozhnikov, D.en
dc.contributor.authorValeev, D.en
dc.date.accessioned2022-05-12T08:28:49Z-
dc.date.available2022-05-12T08:28:49Z-
dc.date.issued2022-
dc.identifier.citationSelective Scandium (Sc) Extraction from Bauxite Residue (Red Mud) Obtained by Alkali Fusion-Leaching Method / A. Shoppert, I. Loginova, J. Napol’skikh et al. // Materials. — 2022. — Vol. 15. — Iss. 2. — 433.en
dc.identifier.issn1996-1944-
dc.identifier.otherAll Open Access, Gold, Green3
dc.identifier.urihttp://elar.urfu.ru/handle/10995/112114-
dc.description.abstractBauxite residue, known as “red mud,” is a potential raw material for extracting rare-earth elements (REEs). The main REEs (Sc, Y, La, Ce, Nd, Nb, and Sm) from the raw bauxite are concentrated in RM after the Bayer leaching process. The earlier worldwide studies were focused on the scandium (Sc) extraction from RM by concentrated acids to enhance the extraction degree. This leads to the dissolution of major oxides (Fe2 O3 and Al2 O3 ) from RM. This article studies the possibility of selective Sc extraction from alkali fusion red mud (RMF) by diluted nitric acid (HNO3 ) leaching at pH ≥ 2 to prevent co-dissolution of Fe2 O3 . RMF samples were analyzed by X-ray fluorescence spectrometry (XRF), X-ray diffraction (XRD), electron probe microanalysis (EPMA), and inductively coupled plasma mass spectrometry (ICP-MS). It was revealed that Sc concentration in RMF can reach up to 140–150 mg kg−1 . Sc extraction was 71.2% at RMF leaching by HNO3 at pH 2 and 80◦ C during 90 min. The leaching solution contained 8 mg L−1 Sc and a high amount of other REEs in the presence of relatively low concentrations of impurity elements such as Fe, Al, Ti, Ca, etc. The kinetic analysis of experimental data by the shrinking core model showed that Sc leaching process is limited by the interfacial diffusion and the diffusion through the product layer. The apparent activation energy (Ea ) was 19.5 kJ/mol. The linear dependence of Sc extraction on magnesium (Mg) extraction was revealed. According to EPMA of RMF, Sc is associated with iron minerals rather than Mg. This allows us to conclude that Mg acts as a leaching agent for the extraction of Sc presented in the RMF in an ion-exchangeable phase. © 2022 by the authors. Licensee MDPI, Basel, Switzerland.en
dc.description.sponsorshipFunding: This work was funded by State Assignment, grant No. 075-03-2021-051/5. The methodology for analysis Sc content in acid solution by ICP-OES was funded by a Ministry of Science and Higher Education of the Russian Federation scientific topic No. 0137-2019-0023. The EPMA analysis was funded by RFBR, grant No. 20-38-90277.en
dc.format.mimetypeapplication/pdfen
dc.language.isoenen
dc.publisherMDPIen1
dc.publisherMDPI AGen
dc.rightsinfo:eu-repo/semantics/openAccessen
dc.sourceMater.2
dc.sourceMaterialsen
dc.subjectACID LEACHINGen
dc.subjectKINETICSen
dc.subjectRARE EARTH ELEMENTSen
dc.subjectSHRINKING CORE MODELen
dc.subjectWASTE RECYCLINGen
dc.subjectACTIVATION ENERGYen
dc.subjectDISSOLUTIONen
dc.subjectELECTRON PROBE MICROANALYSISen
dc.subjectEXTRACTIONen
dc.subjectINDUCTIVELY COUPLED PLASMA MASS SPECTROMETRYen
dc.subjectLEACHINGen
dc.subjectNITRIC ACIDen
dc.subjectRARE EARTHSen
dc.subjectSCANDIUMen
dc.subjectACID LEACHINGen
dc.subjectALKALI FUSIONen
dc.subjectBAUXITE RESIDUEen
dc.subjectELECTRON PROBE MICROANALYSESen
dc.subjectELECTRON-PROBE MICROANALYSISen
dc.subjectLEACHING METHODSen
dc.subjectLEACHING PROCESSen
dc.subjectRED MUDen
dc.subjectSHRINKING CORE MODELen
dc.titleSelective Scandium (Sc) Extraction from Bauxite Residue (Red Mud) Obtained by Alkali Fusion-Leaching Methoden
dc.typeArticleen
dc.typeinfo:eu-repo/semantics/articleen
dc.typeinfo:eu-repo/semantics/publishedVersionen
dc.identifier.rsi47919976-
dc.identifier.doi10.3390/ma15020433-
dc.identifier.scopus85122393900-
local.contributor.employeeShoppert, A., Laboratory of Advanced Technologies in Non-Ferrous and Ferrous Metals Raw Materials Processing, Ural Federal University, Yekaterinburg, 620002, Russian Federation; Loginova, I., Department of Non-Ferrous Metals Metallurgy, Ural Federal University, Yekaterinburg, 620002, Russian Federation; Napol’skikh, J., Department of Non-Ferrous Metals Metallurgy, Ural Federal University, Yekaterinburg, 620002, Russian Federation; Kyrchikov, A., Department of Non-Ferrous Metals Metallurgy, Ural Federal University, Yekaterinburg, 620002, Russian Federation; Chaikin, L., Department of Non-Ferrous Metals Metallurgy, Ural Federal University, Yekaterinburg, 620002, Russian Federation; Rogozhnikov, D., Laboratory of Advanced Technologies in Non-Ferrous and Ferrous Metals Raw Materials Processing, Ural Federal University, Yekaterinburg, 620002, Russian Federation; Valeev, D., Laboratory of Sorption Methods, Vernadsky Institute of Geochemistry and Analytical Chemistry, The Russian Academy of Sciences, Moscow, 119991, Russian Federationen
local.issue2-
local.volume15-
dc.identifier.wos000749925000001-
local.contributor.departmentLaboratory of Advanced Technologies in Non-Ferrous and Ferrous Metals Raw Materials Processing, Ural Federal University, Yekaterinburg, 620002, Russian Federation; Department of Non-Ferrous Metals Metallurgy, Ural Federal University, Yekaterinburg, 620002, Russian Federation; Laboratory of Sorption Methods, Vernadsky Institute of Geochemistry and Analytical Chemistry, The Russian Academy of Sciences, Moscow, 119991, Russian Federationen
local.identifier.pure29376198-
local.description.order433-
local.identifier.eid2-s2.0-85122393900-
local.fund.rffi20-38-90277-
local.identifier.wosWOS:000749925000001-
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