Microkinetic modeling of aqueous phase biomass conversion:Application to ethylene glycol reforming

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dc.contributor.authorGu, Geun Hoko
dc.contributor.authorWittreich, Gerhard R.ko
dc.contributor.authorVlachos, Dionisios G.ko
dc.date.accessioned2019-02-21T01:24:32Z-
dc.date.available2019-02-21T01:24:32Z-
dc.date.created2019-02-18-
dc.date.issued2019-04-
dc.identifier.citationCHEMICAL ENGINEERING SCIENCE, v.197, pp.415 - 418-
dc.identifier.issn0009-2509-
dc.identifier.urihttp://hdl.handle.net/10203/250456-
dc.description.abstractIn this communication, we develop automatically a reaction network for ethylene glycol reforming on Pt. We employ a recently introduced group additivity scheme for estimation of thermochemistry over metal catalysts in vapor phase and in solution along with Bronsted-Evans-Polanyi (BEP) relations for vapor phase kinetics to parameterize microkinetic models for vapor and aqueous phases. Unlike vapor-phase reforming, we show that solvent occupies a significant fraction of surface sites and by doing this, it shifts the water-gas shift reaction to CO2 and H-2 and avoids poisoning of the catalyst by CO. The model is found to be in reasonable agreement with the experimental data. (C) 2019 Elsevier Ltd. All rights reserved.-
dc.languageEnglish-
dc.publisherPERGAMON-ELSEVIER SCIENCE LTD-
dc.titleMicrokinetic modeling of aqueous phase biomass conversion:Application to ethylene glycol reforming-
dc.typeArticle-
dc.identifier.wosid000457634000038-
dc.identifier.scopusid2-s2.0-85060307882-
dc.type.rimsART-
dc.citation.volume197-
dc.citation.beginningpage415-
dc.citation.endingpage418-
dc.citation.publicationnameCHEMICAL ENGINEERING SCIENCE-
dc.identifier.doi10.1016/j.ces.2018.12.036-
dc.contributor.localauthorGu, Geun Ho-
dc.contributor.nonIdAuthorWittreich, Gerhard R.-
dc.contributor.nonIdAuthorVlachos, Dionisios G.-
dc.description.isOpenAccessN-
dc.type.journalArticleArticle-
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