<div class="csl-bib-body">
<div class="csl-entry">Kraussler, M., Binder, M., & Hofbauer, H. (2017). Behavior 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 plant. <i>Biomass Conversion and Biorefinery</i>. https://doi.org/10.1007/s13399-016-0205-y</div>
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The 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>.
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dc.description.abstract
In 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.sponsorship
Austrian Research Promoting Agency (FFG) COMET Bioenergy2020+
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dc.language
English
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dc.language.iso
en
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dc.publisher
Springer
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dc.relation.ispartof
Biomass Conversion and Biorefinery
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dc.rights.uri
http://creativecommons.org/licenses/by/4.0/
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dc.subject
Biomass steam gasification
en
dc.subject
Dual fluidized bed
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dc.subject
Hydrogen
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dc.subject
Product gas
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dc.subject
Water gas shift
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dc.subject
GCMS tar
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dc.title
Behavior 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 plant
en
dc.type
Article
en
dc.type
Artikel
de
dc.rights.license
Creative Commons Namensnennung 4.0 International
de
dc.rights.license
Creative Commons Attribution 4.0 International
en
dc.relation.grantno
C20005 Polygeneration III
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dc.rights.holder
The Author(s) 2016
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dc.type.category
Original Research Article
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tuw.journal.peerreviewed
true
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tuw.peerreviewed
true
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tuw.version
vor
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dcterms.isPartOf.title
Biomass Conversion and Biorefinery
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tuw.publication.orgunit
E166 - Inst. f. Verfahrenstechnik, Umwelttechnik und Techn. Biowissenschaften
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tuw.publisher.doi
10.1007/s13399-016-0205-y
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dc.date.onlinefirst
2016-04-15
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dc.identifier.eissn
2190-6823
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dc.identifier.libraryid
AC11360110
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dc.identifier.urn
urn:nbn:at:at-ubtuw:3-1695
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tuw.author.orcid
0000-0001-6318-9072
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dc.rights.identifier
CC BY 4.0
de
dc.rights.identifier
CC BY 4.0
en
wb.sci
true
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item.fulltext
with Fulltext
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item.openairecristype
http://purl.org/coar/resource_type/c_2df8fbb1
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item.languageiso639-1
en
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item.cerifentitytype
Publications
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item.openaccessfulltext
Open Access
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item.openairetype
research article
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item.grantfulltext
open
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crisitem.author.dept
TU Wien
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crisitem.author.dept
E166 - Institut für Verfahrenstechnik, Umwelttechnik und technische Biowissenschaften