Leaching of Chalcopyrite Concentrate with Hydrogen Peroxide and Sulfuric Acid in an Autoclave System

dc.contributor.authorTuran, M. Deniz
dc.contributor.authorAltundogan, H. Soner
dc.date.accessioned2026-08-12T17:31:56Z
dc.date.issued2013
dc.departmentFırat Üniversitesi
dc.description.abstractIn this study, leaching of chalcopyrite concentrate was investigated in an autoclave system using hydrogen peroxide and sulfuric acid. By decomposition of hydrogen peroxide, the active oxygen formed can provide both high oxidation potential and high pressure in a closed vessel for leaching. Preliminary studies showed that hydrogen peroxide can be used as an oxidant instead of oxygen gas in the autoclave. Central composite design (CCD) was used to examine the effects of the experimental parameters on the copper and iron extraction as a response. The proposed model equation using CCD showed good agreement with experimental data, the correlation coefficients R (2) for copper and iron being 0.84 and 0.86, respectively. The optimum conditions to obtain the main goal of maximum copper and minimum iron extraction from chalcopyrite were determined as to be sulfuric acid concentration of 2.5 M, hydrogen peroxide concentration of 2.3 M, leaching time of 24 minutes, chalcopyrite amount of 3.17 g (in 50-mL solution), stirring speed of 630 rpm, and leaching temperature of 351 K (78 A degrees C). Under the optimum condition, 76 pct of copper and 9 pct of iron were extracted from chalcopyrite concentrate. Extraction yield results of metals indicate that selective leaching of chalcopyrite can be achieved using hydrogen peroxide and sulfuric acid in an autoclave system.
dc.description.sponsorshipTUBITAK (Scientific and Technological Research Council of Turkey) [106M177]
dc.description.sponsorshipThis study was supported by the TUBITAK (Scientific and Technological Research Council of Turkey) under the Project No: 106M177. The authors wish to express their thanks to chemical engineer Hasan Arslanoglu for his help in conducting the experiments. The authors are also thankful to Prof. Dr. Murat Erdemoglu and mining engineer Hakan Derin for help in the SEM analysis.
dc.identifier.doi10.1007/s11663-013-9858-0
dc.identifier.endpage819
dc.identifier.issn1073-5615
dc.identifier.issn1543-1916
dc.identifier.issue4
dc.identifier.orcid0000-0003-3328-9667
dc.identifier.scopus2-s2.0-84880315402
dc.identifier.scopusqualityQ2
dc.identifier.startpage809
dc.identifier.urihttps://doi.org/10.1007/s11663-013-9858-0
dc.identifier.urihttps://hdl.handle.net/11508/56447
dc.identifier.volume44
dc.identifier.wosWOS:000321669900006
dc.identifier.wosqualityQ2
dc.indekslendigikaynakWeb of Science
dc.indekslendigikaynakScopus
dc.language.isoen
dc.publisherSpringer
dc.relation.ispartofMetallurgical and Materials Transactions B-Process Metallurgy and Materials Processing Science
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı
dc.rightsinfo:eu-repo/semantics/closedAccess
dc.snmzKA_WoS_20260511
dc.subjectDissolution Kinetics
dc.subjectFerric Ion
dc.subjectPart Ii
dc.subjectCopper
dc.subjectPressure
dc.subjectChlorination
dc.subjectSulfidation
dc.subjectSphalerite
dc.subjectRecovery
dc.titleLeaching of Chalcopyrite Concentrate with Hydrogen Peroxide and Sulfuric Acid in an Autoclave System
dc.typeArticle

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