DC FieldValueLanguage
dc.contributor.authorKraussler, Michael-
dc.contributor.authorBinder, Matthias-
dc.contributor.authorHofbauer, Hermann-
dc.date.accessioned2020-06-27T15:21:17Z-
dc.date.issued2016-
dc.identifier.issn2190-6823-
dc.identifier.urihttps://resolver.obvsg.at/urn:nbn:at:at-ubtuw:3-1695-
dc.identifier.urihttp://hdl.handle.net/20.500.12708/124-
dc.descriptionThe final publication is available at Springer via <a href="https://doi.org/10.1007/s13399-016-0205-y" target="_blank">https://doi.org/10.1007/s13399-016-0205-y</a>.-
dc.description.abstractIn this paper, the behavior of gas chromatography mass spectroscopy (GCMS) tar components in a three-stage water gas shift (WGS) unit is discussed. The GCMS tar measurements were carried out during the long-term operation (2250 h) of a WGS unit with tar-rich product gas from the commercial biomass steam gasification plant in Oberwart, Austria. In order to investigate the behavior of the GCMS tar components, four tar measurements were performed during the long-term operation of the WGS unit which employed a commercial Fe/Cr-based catalyst. The tar-rich product gas was extracted before reaching the scrubbing unit of the biomass steam gasification plant, therefore, the extracted gas contained a high amount of tar. In order to investigate the behavior of the GCMS tar in the WGS unit, the GCMS tar concentrations were determined at the inlet and the outlet of the WGS unit. The samples were taken during full load operation and during partial load operation of the WGS unit, respectively, the biomass steam gasification plant. In addition to the increase of the volumetric hydrogen content from about 40 % (d.b.) to 50 % (d.b.), the amount of GCMS tar was reduced (up to 38 %) as the gas passed through the WGS unit. No catalyst deactivation was observed. Furthermore, the efficiency of the hydrogen increase or the GCMS tar reduction did not depend on whether the operation of the WGS unit, respectively, the gasification plant was at partial load or full load.en
dc.description.sponsorshipAustrian Research Promoting Agency (FFG) COMET Bioenergy2020+-
dc.languageEnglish-
dc.language.isoen-
dc.publisherSpringer-
dc.relation.ispartofBiomass Conversion and Biorefinery: Processing of Biogenic Material for Energy and Chemistry-
dc.rights.urihttps://creativecommons.org/licenses/by/4.0/-
dc.subjectBiomass steam gasificationen
dc.subjectDual fluidized beden
dc.subjectHydrogenen
dc.subjectProduct gasen
dc.subjectWater gas shiften
dc.subjectGCMS taren
dc.titleBehavior of GCMS tar components in a water gas shift unit operated with tar-rich product gas from an industrial scale dual fluidized bed biomass steam gasification planten
dc.typeArticleen
dc.typeArtikelde
dc.relation.grantnoC20005 Polygeneration III-
dc.rights.holderThe Author(s) 2016-
dc.type.categoryResearch Articleen
dc.type.categoryForschungsartikelde
tuw.versionvor-
dcterms.isPartOf.titleBiomass Conversion and Biorefinery: Processing of Biogenic Material for Energy and Chemistry-
tuw.publication.orgunitE166 - Inst. f. Verfahrenstechnik, Umwelttechnik und Techn. Biowissenschaften-
tuw.publisher.doi10.1007/s13399-016-0205-y-
dc.identifier.libraryidAC11360110-
dc.identifier.urnurn:nbn:at:at-ubtuw:3-1695-
dc.rights.identifierCC BY 4.0-
item.fulltextwith Fulltext-
item.openairetypeArticle-
item.openairetypeArtikel-
item.cerifentitytypePublications-
item.cerifentitytypePublications-
item.languageiso639-1en-
item.grantfulltextopen-
item.openairecristypehttp://purl.org/coar/resource_type/c_18cf-
item.openairecristypehttp://purl.org/coar/resource_type/c_18cf-
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