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dc.contributor.authorGuo, Ning
dc.contributor.authorLi, Tian
dc.contributor.authorZhao, Lihao
dc.contributor.authorLøvås, Terese
dc.date.accessioned2019-11-25T09:45:27Z
dc.date.available2019-11-25T09:45:27Z
dc.date.created2018-11-28T10:09:27Z
dc.date.issued2019
dc.identifier.citationFuel. 2019, 239 636-651.nb_NO
dc.identifier.issn0016-2361
dc.identifier.urihttp://hdl.handle.net/11250/2630185
dc.description.abstractPulverized biomass has great potential to replace coal in many industrial systems such as suspension-firing furnaces and entrained-flow gasifiers. The shape of pulverized biomass deviates significantly from the quasi-spherical coal particle, however, it is common to simulate pulverized biomass particles as spheres as most biomass models are developed based on coal models. With the aim of obtaining a more realistic simulation of pulverized biomass, this work extends the treatment of pulverized biomass to spheroids. A spheroid model that accounts for spheroidal particle drag force and torque was implemented into an Eulerian-Lagrange computational fluid dynamic solver. Comprehensive verifications and validations were performed by comparing with experiments and direct numerical simulations. Furthermore, non-reactive simulations of a lab-scale entrained flow gasifier were carried out using a conventional spherical particle model, a simplified non-sphere model, and the implemented detailed spheroidal particle model. By studying the simulation results of particle and fluid velocities in axial, radial and tangential directions, differences were observed when comparing the sphere model, the simplified non-sphere model, and the spheroid model. The spheroid model shows that particle orientation, which is ignored in the sphere model and the simplified non-sphere model, plays a role in the behavior of the particle dynamics. It was also found that, under such conditions, the spheroid model, compared to the sphere model, yields a more dispersed distribution regarding the particle residence time and local concentration. These non-reactive simulation results imply that shortcomings may exist in the common practice of simulating conversion of pulverized biomass in which the sphere model or the simplified non-sphere model is applied.nb_NO
dc.language.isoengnb_NO
dc.publisherElseviernb_NO
dc.relation.urihttps://www.sciencedirect.com/science/article/pii/S0016236118318672
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internasjonal*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/deed.no*
dc.titleEulerian-Lagrangian simulation of pulverized biomass jet using spheroidal particle approximationnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionacceptedVersionnb_NO
dc.source.pagenumber636-651nb_NO
dc.source.volume239nb_NO
dc.source.journalFuelnb_NO
dc.identifier.doi10.1016/j.fuel.2018.10.137
dc.identifier.cristin1636180
dc.relation.projectNorges forskningsråd: 244069nb_NO
dc.relation.projectNorges forskningsråd: 250146nb_NO
dc.description.localcode© 2018. This is the authors’ accepted and refereed manuscript to the article. Locked until 29.11.2020 due to copyright restrictions. This manuscript version is made available under the CC-BY-NC-ND 4.0 license http://creativecommons.org/licenses/by-nc-nd/4.0/nb_NO
cristin.unitcode194,64,25,0
cristin.unitnameInstitutt for energi- og prosessteknikk
cristin.ispublishedtrue
cristin.fulltextpostprint
cristin.qualitycode2


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Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal
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