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dc.contributor.authorSurup, Gerrit Ralf
dc.contributor.authorFoppe, Manuel
dc.contributor.authorSchubert, Daniel
dc.contributor.authorDeike, Rüdiger
dc.contributor.authorHeidelmann, Markus
dc.contributor.authorTimko, Michael T.
dc.contributor.authorTrubetskaya, Anna
dc.date.accessioned2018-10-03T12:24:39Z
dc.date.available2018-10-03T12:24:39Z
dc.date.created2018-09-28T22:49:17Z
dc.date.issued2019
dc.identifier.citationFuel. 2019, 235 306-316.nb_NO
dc.identifier.issn0016-2361
dc.identifier.urihttp://hdl.handle.net/11250/2566175
dc.description.abstractThis study reports the effect of feedstock origin, residence time, and heat treatment temperature on CO2 and O2 reactivities, nanostructure and carbon chemistry of chars prepared at 1300, 1600, 2400, and 2800 °C in a slow pyrolysis reactor. The structure of char was characterized by transmission electron microscopy and Raman spectroscopy. The CO2 and O2 reactivity of char was investigated by thermogravimetric analysis. Results showed that the ash composition and residence time influence the char reactivity less than the heat treatment temperature. The heat treatment temperature and co-pyrolysis of pinewood char with biooil decreased the CO2 reactivity, approaching that of metallurgical coke. Importantly from a technological standpoint, the reactivities of char from high temperature pyrolysis (2400–2800 °C) were similar to those of metallurgical coke, emphasizing the importance of graphitizing temperatures on the char behavior. Moreover, graphitization of chars from wood and herbaceous biomass increased with the increasing heat treatment temperature, leading to formation of graphitizing carbon.
dc.language.isoengnb_NO
dc.titleThe effect of feedstock origin and temperature on the structure and reactivity of char from pyrolysis at 1300–2800 °Cnb_NO
dc.title.alternativeThe effect of feedstock origin and temperature on the structure and reactivity of char from pyrolysis at 1300–2800 °Cnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionpublishedVersionnb_NO
dc.source.pagenumber306-316nb_NO
dc.source.volume235nb_NO
dc.source.journalFuelnb_NO
dc.identifier.doihttps://doi.org/10.1016/j.fuel.2018.07.093
dc.identifier.cristin1616024
dc.description.localcodeNivå2nb_NO
cristin.unitcode201,15,3,0
cristin.unitnameInstitutt for ingeniørvitenskap
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode2


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