Publication:
Catalytic Deoxygenation of Oleic Acid Over Synthesized Ni@CMK-3 Catalyst Using Analytical Py-GC/MS and TG-FTIR

dc.authorscopusid57205605969
dc.authorscopusid7003728792
dc.authorscopusid7005672307
dc.authorwosidCeylan, Selim/Lsj-5591-2024
dc.authorwosidÇakman, Gülce/Abd-8667-2020
dc.contributor.authorÇakman, Gülce
dc.contributor.authorCeylan, Selim
dc.contributor.authorBalci, Suna
dc.date.accessioned2025-12-11T00:42:52Z
dc.date.issued2023
dc.departmentOndokuz Mayıs Üniversitesien_US
dc.department-temp[Cakman, Gulce; Balci, Suna] Gazi Univ, Fac Engn, Chem Engn Dept, TR-06570 Ankara, Turkey; [Cakman, Gulce; Ceylan, Selim] Ondokuz Mayis Univ, Fac Engn, Chem Engn Dept, TR-55139 Samsun, Turkeyen_US
dc.description.abstractConverting waste oils into renewable fuels by catalytic deoxygenation reactions is a promising method to achieve pollution reduction and resource recovery. In this study, Ni@CMK-3 catalyst was synthesized by impregnation method and its performance in oleic acid (OA) pyrolysis which follows deoxygenation reactions was investigated. The silica template (SBA-15), carbon support (CMK-3) and catalyst (Ni@CMK-3) were characterized using XRD patterns, N-2 adsorption/desorption isotherms, Raman spectra, SEM images and ICP-MS analysis. XRD results showed that CMK-3 had uniform hexagonal arrays and metal loading on support did not affect this structure. Nickel loading (20% by mass) to CMK-3 was proven by both ICP-MS (21.6%) and SEM/EDS (17.4%) results. The surface area values were found as 778 m(2)/g for SBA-15; 1461 and 1332 m(2)/g for CMK-3 and Ni@CMK-3, respectively. Non-catalytic and catalytic (OA:catalyst = 1:1 by mass) pyrolysis tests were performed using py-GC/MS. In non-catalytic reaction, OA conversion was low while in the catalytic reaction the value was increased at a temperature of 350 C-o at which hydrocarbons and several acids (2-propenoic acid, hexadecanoic acid etc.) were the most common products in both. These results were also confirmed with TG-FTIR results. The study showed that Ni@CMK-3 catalyst was suitable for OA pyrolysis to produce biofuels.en_US
dc.description.sponsorshipScientific and Technological Research Council of Turkey (TUBITAK) [119M814]en_US
dc.description.sponsorshipPartial financial support was received from Scientific and Technological Research Council of Turkey (TUBITAK) with a project code of 119M814.en_US
dc.description.woscitationindexScience Citation Index Expanded
dc.identifier.doi10.1007/s10934-022-01392-1
dc.identifier.endpage909en_US
dc.identifier.issn1380-2224
dc.identifier.issn1573-4854
dc.identifier.issue3en_US
dc.identifier.scopus2-s2.0-85142505410
dc.identifier.scopusqualityQ2
dc.identifier.startpage899en_US
dc.identifier.urihttps://doi.org/10.1007/s10934-022-01392-1
dc.identifier.urihttps://hdl.handle.net/20.500.12712/38680
dc.identifier.volume30en_US
dc.identifier.wosWOS:000888715100001
dc.identifier.wosqualityQ2
dc.language.isoenen_US
dc.publisherSpringeren_US
dc.relation.ispartofJournal of Porous Materialsen_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.subjectCMK-3en_US
dc.subjectNickel Impregnationen_US
dc.subjectCharacterizationen_US
dc.subjectPyrolysisen_US
dc.subjectOleic Aciden_US
dc.subjectBiofuelen_US
dc.titleCatalytic Deoxygenation of Oleic Acid Over Synthesized Ni@CMK-3 Catalyst Using Analytical Py-GC/MS and TG-FTIRen_US
dc.typeArticleen_US
dspace.entity.typePublication

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