Приказ основних података о документу

dc.creatorOlewski, Tomasz
dc.creatorTodić, Branislav
dc.creatorNowicki, Lech
dc.creatorNikačević, Nikola
dc.creatorBukur, Dragomir B.
dc.date.accessioned2021-03-10T12:43:58Z
dc.date.available2021-03-10T12:43:58Z
dc.date.issued2015
dc.identifier.issn0263-8762
dc.identifier.urihttp://TechnoRep.tmf.bg.ac.rs/handle/123456789/2972
dc.description.abstractTwo kinetic models of Fischer-Tropsch product selectivity have been developed based on reaction networks from the literature. The models were fitted to experimental data obtained using commercial iron-based catalyst in a stirred tank slurry reactor and under a wide range of process conditions. Results showed that both of the rival models were able to provide a satisfactory prediction of the experimental product distribution for n-paraffin, 1- and 2-olefin. The simpler of the two models, a reaction network with a single type of active sites and solubility enhanced 1-olefin readsorption term, was chosen as more adequate for practical use.en
dc.publisherElsevier, Amsterdam
dc.relationUS DOEUnited States Department of Energy (DOE) [DE-FG26-02NT41540]
dc.relationQatar Foundation
dc.relationinfo:eu-repo/grantAgreement/MESTD/Basic Research (BR or ON)/172022/RS//
dc.rightsopenAccess
dc.sourceChemical Engineering Research & Design
dc.subjectFischer-Tropsch synthesisen
dc.subjectKinetic modelen
dc.subjectIron catalysten
dc.subjectProduct selectivityen
dc.subjectOlefin readsorptionen
dc.titleHydrocarbon selectivity models for iron-based Fischer-Tropsch catalysten
dc.typearticle
dc.rights.licenseARR
dc.citation.epage11
dc.citation.other95: 1-11
dc.citation.rankM21
dc.citation.spage1
dc.citation.volume95
dc.identifier.doi10.1016/j.cherd.2014.12.015
dc.identifier.fulltexthttp://TechnoRep.tmf.bg.ac.rs/bitstream/id/998/2969.pdf
dc.identifier.scopus2-s2.0-84975806611
dc.identifier.wos000351966600001
dc.type.versionpublishedVersion


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Приказ основних података о документу