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dc.contributor.authorChiremba, Elijah
dc.contributor.authorZhang, Kui
dc.contributor.authorKazak, Canan
dc.contributor.authorAkay, Galip
dc.date.accessioned2020-06-21T13:18:15Z
dc.date.available2020-06-21T13:18:15Z
dc.date.issued2017
dc.identifier.issn0001-1541
dc.identifier.issn1547-5905
dc.identifier.urihttps://doi.org/10.1002/aic.15769
dc.identifier.urihttps://hdl.handle.net/20.500.12712/12232
dc.descriptionKazak, Canan/0000-0003-2475-8775en_US
dc.descriptionWOS: 000409146600014en_US
dc.description.abstractDirect nonoxidative conversion of methane to hydrogen and hydrocarbons was achieved at atmospheric pressure and 120 degrees C using nonthermal plasma sustained by plasma catalysis promoters (PCPs). Reactors had two different electrode configurations. Methane conversion correlated well with the specific energy density (SED). Methane conversion was independent of plasma power, flow rate, electrode configuration, or the type of PCPs. Hydrogen selectivity (ca. 60%) was dependent significantly on PCP and electrode configuration. The ethane/ethylene molar ratio increased from 0 to 0.15 with increasing SED. When the SED value was below ca. 100 kJ/L, ethylene was the only C-2 hydrocarbon. These results are similar to the recently reported nonoxidative catalytic methane conversion at ca. 1000 degrees C. Therefore, these results represent process intensification in methane conversion. PCPs underwent structural and chemical changes but their performances are not affected during an 80-h experimental period. (c) 2017 American Institute of Chemical Engineers AIChE J, 63: 4418-4429, 2017en_US
dc.description.sponsorshipEU project under Framework Programme 7, FP7 [CP-IP 228853]; EUEuropean Union (EU); Turkish Scientific and Technical Research Council, TUBITAKTurkiye Bilimsel ve Teknolojik Arastirma Kurumu (TUBITAK) [BIDEB 2236]; TUBITAKTurkiye Bilimsel ve Teknolojik Arastirma Kurumu (TUBITAK)en_US
dc.description.sponsorshipThe research contained in this was supported by an EU project under Framework Programme 7, FP7, (grant agreement no. CP-IP 228853 under the project title COPIRIDE: Combining Process Intensificationdriven Manufacture of Microstructured Reactors and Process Design regarding to Industrial Dimensions and Environment) directed by Prof. Galip Akay at Newcastle University. The research was completed and further extended through another EU-grant (Prof. Galip Akay and Prof. Canan Kazak) administered by the Turkish Scientific and Technical Research Council, TUBITAK (grant reference BIDEB 2236). These grants are gratefully acknowledged. The authors also acknowledge the support from TUBITAK for Prof. Kazak during her Visiting Professorship at Newcastle University. They are grateful to Mr. Yunus Gedik for the use of SEM and EDX facilities at KITAM.en_US
dc.language.isoengen_US
dc.publisherWileyen_US
dc.relation.isversionof10.1002/aic.15769en_US
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.subjectcatalysisen_US
dc.subjectfuelsen_US
dc.subjecthydrocarbon processingen_US
dc.subjectpetroleumen_US
dc.subjectplasmaen_US
dc.titleDirect nonoxidative conversion of methane to hydrogen and higher hydrocarbons by dielectric barrier discharge plasma with plasma catalysis promotersen_US
dc.typearticleen_US
dc.contributor.departmentOMÜen_US
dc.identifier.volume63en_US
dc.identifier.issue10en_US
dc.identifier.startpage4418en_US
dc.identifier.endpage4429en_US
dc.relation.journalAiche Journalen_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US


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