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dc.contributor.authorGholami, Zahra
dc.contributor.authorGholami, Fatemeh
dc.contributor.authorTišler, Zdeněk
dc.contributor.authorHubáček, Jan
dc.contributor.authorTomáš, Martin
dc.contributor.authorBačiak, Miroslav
dc.contributor.authorVakili, Mohammadtaghi
dc.date.accessioned2022-09-12T10:00:24Z-
dc.date.available2022-09-12T10:00:24Z-
dc.date.issued2022
dc.identifier.citationGHOLAMI, Z. GHOLAMI, F. TIŠLER, Z. HUBÁČEK, J. TOMÁŠ, M. BAČIAK, M. VAKILI, M. Production of Light Olefins via Fischer-Tropsch Process Using Iron-Based Catalysts: A Review. Catalysts, 2022, roč. 12, č. 2, s. nestránkováno. ISSN: 2073-4344cs
dc.identifier.issn2073-4344
dc.identifier.uri2-s2.0-85123518883
dc.identifier.urihttp://hdl.handle.net/11025/49641
dc.format34 s.cs
dc.format.mimetypeapplication/pdf
dc.language.isoenen
dc.publisherMDPIen
dc.relation.ispartofseriesCatalystsen
dc.rights© authorsen
dc.titleProduction of Light Olefins via Fischer-Tropsch Process Using Iron-Based Catalysts: A Reviewen
dc.typečlánekcs
dc.typearticleen
dc.rights.accessopenAccessen
dc.type.versionpublishedVersionen
dc.description.abstract-translatedThe production of light olefins, as the critical components in chemical industries, is possible via different technologies. The Fischer–Tropsch to olefin (FTO) process aims to convert syngas to light olefins with high selectivity over a proper catalyst, reduce methane formation, and avoid the production of excess CO2. This review describes the production of light olefins through the FTO process using both unsupported and supported iron‐based catalysts. The catalytic properties and performances of both the promoted and bimetallic unsupported catalysts are reviewed. The effect of support and its physico‐chemical properties on the catalyst activity are also described. The proper catalyst should have high stability to provide long‐term performance without reducing the activity and selectivity towards the desired product. The good dispersion of active metals on the surface, proper porosity, optimized metal‐support interaction, a high degree of reducibility, and providing a sufficient active phase for the reaction are important parameters affecting the reaction. The selection of the suitable catalyst with enhanced activity and the optimum process conditions can increase the possibility of the FTO reaction for light‐olefins production. The production of light olefins via the FTO process over iron‐based catalysts is a promising method, as iron is cheap, shows higher resistance to sulfur, and has a higher WGS activity which can be helpful for the feed gas with a low H2/CO ratio, and also has higher selectivity towards light olefins.en
dc.subject.translatedolefin productionen
dc.subject.translatedFischer–Tropschen
dc.subject.translatediron catalysten
dc.subject.translatedpromoteren
dc.subject.translatedsupporten
dc.identifier.doi10.3390/catal12020174
dc.type.statusPeer-revieweden
dc.identifier.document-number773042800001
dc.identifier.obd43936520
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