The Investigation of Metallic Silver Dissolution Kinetics Using DL-Malic Acid with Hydrogen Peroxide Solution as an Eco-Friendly Leaching System: The Rotating Disc Method

dc.contributor.authorMotasim, Mahmoud
dc.contributor.authorBoyrazli, Mustafa
dc.contributor.authorAydogan, Salih
dc.contributor.authorAgacayak, Tevfik
dc.contributor.authorAli, Babiker
dc.date.accessioned2026-08-12T17:26:59Z
dc.date.issued2025
dc.departmentFırat Üniversitesi
dc.description.abstractAlthough cyanidation remains widely employed for silver recovery due to its cost-effectiveness, it presents serious environmental and health hazards. In this study, the dissolution kinetics of silver were investigated in an environmentally benign leaching system composed of DL-malic acid and hydrogen peroxide, employing the rotating disc method. High-purity silver discs (99.99 pct) were used to examine the effects of rotation speed, disc surface area, temperature, and the concentrations of DL-malic acid and hydrogen peroxide on the leaching rate. X-ray diffraction (XRD) and Fourier-transform infrared spectroscopy (FTIR) were conducted to characterize the silver surface before and after leaching. Additionally, contact angle measurements were performed to evaluate the interfacial interaction between the leaching solution and the silver surface. The results demonstrated that the dissolution rate increased with temperature, rotation speed, hydrogen peroxide concentration, and surface area. However, elevated concentrations of DL-malic acid resulted in the formation of a passivating layer on the silver surface, likely due to chelation effects, which significantly impeded the access of protons (H+) to the silver surface, thereby reducing the dissolution rate. Contact angle analysis further indicated reduced wettability at higher DL-malic acid concentrations, with values reaching up to 87.80 deg. XRD analysis confirmed the partial oxidation of the silver surface, forming Ag2O. The reaction was determined to be chemically controlled, with an activation energy of 44.14 kJ/mol.
dc.identifier.doi10.1007/s11663-025-03714-5
dc.identifier.endpage5518
dc.identifier.issn1073-5615
dc.identifier.issn1543-1916
dc.identifier.issue5
dc.identifier.orcid0000-0001-8120-8804
dc.identifier.scopus2-s2.0-105011348594
dc.identifier.scopusqualityQ2
dc.identifier.startpage5509
dc.identifier.urihttps://doi.org/10.1007/s11663-025-03714-5
dc.identifier.urihttps://hdl.handle.net/11508/55037
dc.identifier.volume56
dc.identifier.wosWOS:001534309900001
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/openAccess
dc.snmzKA_WoS_20260511
dc.subjectCitric-Acid
dc.subjectCyanidation
dc.subjectGold
dc.subjectRecovery
dc.subjectConcentrate
dc.subjectBehavior
dc.subjectThiourea
dc.subjectLithium
dc.subjectOxidant
dc.subjectAlloys
dc.titleThe Investigation of Metallic Silver Dissolution Kinetics Using DL-Malic Acid with Hydrogen Peroxide Solution as an Eco-Friendly Leaching System: The Rotating Disc Method
dc.typeArticle

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