Zobrazit minimální záznam

dc.contributor.authorČarnogurská, Mária
dc.contributor.authorPříhoda, Miroslav
dc.contributor.authorLázár, Marián
dc.contributor.authorKurilla, Peter
dc.date.accessioned2018-05-04T09:21:25Z
dc.date.available2018-05-04T09:21:25Z
dc.date.issued2018
dc.identifier.citationMateriali in Tehnologije. 2018, vol. 52, no. 2, p. 133-138.cs
dc.identifier.issn1580-2949
dc.identifier.issn1580-3414
dc.identifier.urihttp://hdl.handle.net/10084/126688
dc.description.abstractThe following article describes the thermal process for the recovery of used silver from Ag catalysts using an 80-kVA plasma reactor, along with an appropriate flux and reducing agent. An Ag catalyst was melted in three separate experiments with different weights. The overall recovery of silver from the melted Ag catalysts was high (93.8-96.4) %. The byproducts of the melting of the Ag catalysts were the inert vitrified slag, synthesis gas and fly ash. The chemical analysis of fly ash confirmed that, in addition to mechanically stripped oxides that were present in the batch (CaO, SiO2, MgO, and Al2O3), fly ash also contained a high amount of condensed silver. Indeed, silver evaporated at a high temperature during the melting process. The silver condensed in fly ash was at a level of 37.08-48.37 % of the total weight of fly ash. Therefore, fly ash had to be recycled. The synthesis gas from the process had a relatively low heating value (0.6335 MJ m(-3)).cs
dc.format.extent584645 bytes
dc.format.mimetypeapplication/pdf
dc.language.isoencs
dc.publisherInštitut za kovinske materiale in tehnologijecs
dc.relation.ispartofseriesMateriali in Tehnologijecs
dc.relation.urihttps://doi.org/10.17222/mit.2017.050cs
dc.rights© MATERIALI IN TEHNOLOGIJEcs
dc.subjecthazardous wastecs
dc.subjectAg catalystcs
dc.subjectplasma technologycs
dc.titlePyrometallurgical treatment of silver-containing catalystscs
dc.title.alternativePirometalurška obdelava katalizatorja z vsebnostjo srebracs
dc.typearticlecs
dc.description.abstract-enČlanek opisuje termični način pridobivanja srebra iz rabljenih Ag katalizatorjev v 80 kVA plazemskem reaktorju v prisotnosti ustreznih talil in redukcijskega sredstva. Ag katalizator se je talil v treh poskusih z različno maso. Skupi iznos srebra pri procesu taljenja Ag katalizatorjev je bil visok (od 93,8 % do 96,4 %). Pri taljenju katalizatorja je nastajala inertna vitrificirana žlindra, sintezni plin in ostale ubežne emisije. Kemična analiza ubežnih emisij je potrdila, da so poleg mehansko odtrganih oksidov iz vhodnega materiala (CaO, SiO2, MgO, Al2O3) vsebovale tudi višjo vsebnost kondenziranega srebra. Srebro je v procesu taljenja izparelo pri visoki temperaturi. V ubežnih emisijah kondenzirano srebro je bilo na nivoju od 37,08 % do 48,37 %. Ubežne emisije je bilo treba zato reciklirati. S procesom pridobljeni sintezni plin je bil razmeroma nizke kalorične vrednosti (0.6335 MJ m–3).cs
dc.identifier.doi10.17222/mit.2017.050
dc.rights.accessopenAccesscs
dc.type.versionpublishedVersioncs
dc.type.statusPeer-reviewedcs
dc.description.sourceWeb of Sciencecs
dc.description.volume52cs
dc.description.issue2cs
dc.description.lastpage138cs
dc.description.firstpage133cs
dc.identifier.wos000430301300005


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Zobrazit minimální záznam