Vis enkel innførsel

dc.contributor.authorMa, Wenping
dc.contributor.authorShafer, Wilson D.
dc.contributor.authorJacobs, Gary
dc.contributor.authorYang, Jia
dc.contributor.authorSparks, Dennis E.
dc.contributor.authorHamdeh, Hussein H.
dc.contributor.authorDavis, Burtron H.
dc.date.accessioned2019-03-12T12:24:45Z
dc.date.available2019-03-12T12:24:45Z
dc.date.created2018-10-31T20:51:26Z
dc.date.issued2018
dc.identifier.citationApplied Catalysis A : General. 2018, 560 144-152.nb_NO
dc.identifier.issn0926-860X
dc.identifier.urihttp://hdl.handle.net/11250/2589700
dc.description.abstractThe explanation for CH4 selectivity for iron based Fischer-Tropsch catalysts in the low conversion region (i.e., <50%) remains elusive. In this contribution, the CO conversion effect was carefully examined over four K promoted Fe catalysts (100 Fe/5.1Si/2Cu/ x K, where x = 1–5) over a wide range of CO conversion (i.e., 4–85%). Moreover, the effect of CO conversion on oxygenate selectivity of the Fe-K catalysts was carefully studied as well. The change in CH4 selectivity with CO conversion was found to resemble asymmetric “V” shaped curves, with the minimum values occurring at approximately 50% CO conversion. Adding greater than x  = 2 K significantly alleviated the CO conversion effect which was attributed to the high K loading greatly decreasing the surface H coverage while improving CO adsorption. The unique CH4 selectivity trend suggests a complicated CH4 formation process that results from different aspects of the catalyst (i.e., chain growth and hydrogenation rates), and process conditions. Oxygenate selectivity was in the range of 0.7–2.8% and varied with the CO conversion and K loading. The addition of K up to x  = 3 was found to promote oxygenate formation and chain growth. The overall oxygenate distribution up to C17 follows an Anderson-Schulz Flory (ASF) distribution, with ethanol being the dominant oxygenate. Mechanisms of oxygenate formation different from that of hydrocarbon formation (e.g., CO insertion versus CO dissociation) were proposed to explain the experimental results.nb_NO
dc.language.isoengnb_NO
dc.publisherElseviernb_NO
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internasjonal*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/deed.no*
dc.titleFischer-Tropsch synthesis: Effect of CO conversion on CH4 and oxygenate selectivities over precipitated Fe-K catalystsnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionacceptedVersionnb_NO
dc.source.pagenumber144-152nb_NO
dc.source.volume560nb_NO
dc.source.journalApplied Catalysis A : Generalnb_NO
dc.identifier.doi10.1016/j.apcata.2018.04.042
dc.identifier.cristin1625692
dc.description.localcode© 2018. This is the authors’ accepted and refereed manuscript to the article. Locked until 30.04.2020 due to copyright restrictions. This manuscript version is made available under the CC-BY-NC-ND 4.0 license http://creativecommons.org/licenses/by-nc-nd/4.0/nb_NO
cristin.unitcode194,66,30,0
cristin.unitnameInstitutt for kjemisk prosessteknologi
cristin.ispublishedtrue
cristin.fulltextpostprint
cristin.qualitycode1


Tilhørende fil(er)

Thumbnail

Denne innførselen finnes i følgende samling(er)

Vis enkel innførsel

Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal
Med mindre annet er angitt, så er denne innførselen lisensiert som Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal