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dc.contributor.authorShoppert, A.en
dc.contributor.authorValeev, D.en
dc.contributor.authorLoginova, I.en
dc.contributor.authorChaikin, L.en
dc.contributor.authorPan, J.en
dc.date.accessioned2024-04-05T16:34:50Z-
dc.date.available2024-04-05T16:34:50Z-
dc.date.issued2023-
dc.identifier.citationShoppert, A, Valeev, D, Loginova, I, Chaikin, L & Pan, J 2023, 'Enhanced Coal Fly Ash Desilication Using Atmospheric NaOH Leaching with Simultaneous Magnetic Separation', Metals, Том. 13, № 10, 1647. https://doi.org/10.3390/met13101647harvard_pure
dc.identifier.citationShoppert, A., Valeev, D., Loginova, I., Chaikin, L., & Pan, J. (2023). Enhanced Coal Fly Ash Desilication Using Atmospheric NaOH Leaching with Simultaneous Magnetic Separation. Metals, 13(10), [1647]. https://doi.org/10.3390/met13101647apa_pure
dc.identifier.issn2075-4701-
dc.identifier.otherFinal2
dc.identifier.otherAll Open Access, Gold3
dc.identifier.otherhttps://www.scopus.com/inward/record.uri?eid=2-s2.0-85174891940&doi=10.3390%2fmet13101647&partnerID=40&md5=9d5ce6b530a6c39e9244f14a1ebb89641
dc.identifier.otherhttps://www.mdpi.com/2075-4701/13/10/1647/pdf?version=1695656512pdf
dc.identifier.urihttp://elar.urfu.ru/handle/10995/130878-
dc.description.abstractCoal fly ash (CFA) is a technogenic waste formed during coal combustion in thermal power plants (TPPs). The extraction of valuable components from CFA is complicated by the presence of a large amount of amorphous glassy mass and iron. Herein, a novel method of CFA desilication with complete extraction of the amorphous glassy mass without desilication product (DSP) precipitation and simultaneous magnetic fraction recovery in one stage is presented. The Fe recovery in the magnetic fraction using the proposed method was significantly improved from 52% to 68%. After conventional wet magnetic separation, followed by the proposed method for desilication and magnetic fraction separation, the Fe recovery was increased to 73.8%. Because of the absence of DSP precipitation, the Na2O content in the solid residue after desilication was lower than 1 wt.%. The simultaneous desilication and magnetic separation of magnetite was achieved by installing a belt of permanent magnets on the outer surface of the reactor, where the CFA was leached by the highly concentrated NaOH solution. The effects of different parameters on the extraction of Si, Al, and Fe from the raw CFA were elucidated by varying the liquid-to-solid ratio (L:S ratio) from 5 to 10, the temperature from 100 to 120 °C, the leaching time from 10 to 30 min, and the particle size from −50 µm to −73 µm. The optimal leaching parameters were determined to be temperature = 110 °C, L:S ratio = 7.5, and leaching time = 20 min. The extraction of Si and Fe under these conditions was higher than 66 and 73%, respectively. The Al extraction was lower than 10%. The solid residue of NaOH leaching and the magnetic fraction were examined by X-ray diffraction, X-ray fluorescence spectrometry, vibrating sample magnetometry, scanning electron microscopy with energy-dispersive X-ray spectroscopy, Brunauer–Emmett–Teller, and laser diffraction analyses. © 2023 by the authors.en
dc.description.sponsorshipRussian Science Foundation, RSF: 22-23-20150en
dc.description.sponsorshipThis research was supported by the Russian Science Foundation and Government of Sverdlovsk region, Joint Grant No. 22-23-20150.en
dc.format.mimetypeapplication/pdfen
dc.language.isoenen
dc.publisherMultidisciplinary Digital Publishing Institute (MDPI)en
dc.relationinfo:eu-repo/grantAgreement/RSF//22-23-20150en
dc.rightsinfo:eu-repo/semantics/openAccessen
dc.rightscc-byother
dc.rights.urihttps://creativecommons.org/licenses/by/4.0/unpaywall
dc.sourceMetals2
dc.sourceMetalsen
dc.subjectALKALINE LEACHINGen
dc.subjectCOAL FLY ASHen
dc.subjectDESILICATIONen
dc.subjectIRON EXTRACTIONen
dc.subjectKINETICSen
dc.subjectWASTE UTILIZATIONen
dc.titleEnhanced Coal Fly Ash Desilication Using Atmospheric NaOH Leaching with Simultaneous Magnetic Separationen
dc.typeArticleen
dc.typeinfo:eu-repo/semantics/articleen
dc.type|info:eu-repo/semantics/publishedVersionen
dc.identifier.doi10.3390/met13101647-
dc.identifier.scopus85174891940-
local.contributor.employeeShoppert, A., Department of Non-Ferrous Metals Metallurgy, Ural Federal University, Yekaterinburg, 620002, Russian Federationen
local.contributor.employeeValeev, D., Laboratory of Sorption Methods, Vernadsky Institute of Geochemistry and Analytical Chemistry of the Russian Academy of Sciences, Moscow, 119991, Russian Federationen
local.contributor.employeeLoginova, I., Department of Non-Ferrous Metals Metallurgy, Ural Federal University, Yekaterinburg, 620002, Russian Federationen
local.contributor.employeeChaikin, L., Department of Non-Ferrous Metals Metallurgy, Ural Federal University, Yekaterinburg, 620002, Russian Federationen
local.contributor.employeePan, J., Key Laboratory of Coal Processing and Efficient Utilization, Ministry of Education, School of Chemical Engineering and Technology, China University of Mining and Technology, Xuzhou, 221116, Chinaen
local.issue10-
local.volume13-
dc.identifier.wos001089535700001-
local.contributor.departmentDepartment of Non-Ferrous Metals Metallurgy, Ural Federal University, Yekaterinburg, 620002, Russian Federationen
local.contributor.departmentLaboratory of Sorption Methods, Vernadsky Institute of Geochemistry and Analytical Chemistry of the Russian Academy of Sciences, Moscow, 119991, Russian Federationen
local.contributor.departmentKey Laboratory of Coal Processing and Efficient Utilization, Ministry of Education, School of Chemical Engineering and Technology, China University of Mining and Technology, Xuzhou, 221116, Chinaen
local.identifier.pure47866873-
local.description.order1647-
local.identifier.eid2-s2.0-85174891940-
local.fund.rsf22-23-20150-
local.identifier.wosWOS:001089535700001-
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