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dc.contributor.authorGavrilovic, Ljubisa
dc.contributor.authorBrandin, Jan
dc.contributor.authorHolmen, Anders
dc.contributor.authorVenvik, Hilde Johnsen
dc.contributor.authorMyrstad, Rune
dc.contributor.authorBlekkan, Edd Anders
dc.date.accessioned2018-02-22T12:11:50Z
dc.date.available2018-02-22T12:11:50Z
dc.date.created2018-02-15T12:22:37Z
dc.date.issued2018
dc.identifier.citationIndustrial & Engineering Chemistry Research. 2018, 57 1935-1942.nb_NO
dc.identifier.issn0888-5885
dc.identifier.urihttp://hdl.handle.net/11250/2486443
dc.description.abstractA 20%Co/0.5%Re/γAl2O3 Fischer−Tropsch catalyst was poisoned by four potassium salts (KNO3, K2SO4, KCl, and K2CO3) using the aerosol deposition technique, depositing up to 3500 ppm K as solid particles. Standard characterization techniques (H2 chemisorption, BET, TPR) showed no difference between treated samples and their unpoisoned counterpart. The Fischer−Tropsch activity was investigated at industrially relevant conditions (210 °C, H2:CO = 2:1, 20 bar). The catalytic activity was significantly reduced for samples exposed to potassium, and the loss of activity was more severe with higher potassium loadings, regardless of the potassium salt used. A possible dual deactivation effect by potassium and the counterion (chloride and sulfate) is observed with the samples poisoned by KCl and K2SO4. The selectivity toward heavier hydrocarbons (C5+) was slightly increased with increasing potassium loading, while the CH4 selectivity was reduced for all the treated samples. The results support the idea that potassium is mobile under FT conditions. The loss of activity was described by simple deactivation models.nb_NO
dc.language.isoengnb_NO
dc.publisherAmerican Chemical Societynb_NO
dc.subjectGassifisering av biomassenb_NO
dc.subjectBiomass gasificationnb_NO
dc.subjectHeterogen katalysenb_NO
dc.subjectHeterogeneous Catalysisnb_NO
dc.titleDeactivation of Co-Based Fischer−Tropsch Catalyst by Aerosol Deposition of Potassium Saltsnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionacceptedVersionnb_NO
dc.subject.nsiVDP::Kjemiteknikk: 563nb_NO
dc.subject.nsiVDP::Chemical engineering unit operations: 563nb_NO
dc.source.pagenumber1935-1942nb_NO
dc.source.volume57nb_NO
dc.source.journalIndustrial & Engineering Chemistry Researchnb_NO
dc.identifier.doi10.1021/acs.iecr.7b04498
dc.identifier.cristin1565503
dc.relation.projectNorges forskningsråd: 228741nb_NO
dc.description.localcode© American Chemical Society 2018. This is the authors accepted and refereed manuscript to the article. Locked until 23.1.2019 due to copyright restrictions.nb_NO
cristin.unitcode194,66,30,0
cristin.unitnameInstitutt for kjemisk prosessteknologi
cristin.ispublishedtrue
cristin.fulltextpostprint
cristin.qualitycode2


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