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dc.contributor.authorAgu, Cornelius Emeka
dc.contributor.authorPfeifer, Christoph
dc.contributor.authorMoldestad, Britt Margrethe Emilie
dc.date.accessioned2020-02-18T14:17:25Z
dc.date.available2020-02-18T14:17:25Z
dc.date.created2019-07-02T21:12:54Z
dc.date.issued2019
dc.identifier.citationPowder Technology. 2019, 349 99-107.
dc.identifier.issn0032-5910
dc.identifier.urihttps://hdl.handle.net/11250/2642370
dc.description.abstractFor operational control and design of a fluidized bed reactor containing different types of solid particles, the bed void fraction and minimum fluidization velocity are vital parameters. This paper demonstrates a method for predicting the void fraction and minimum fluidization velocity of different binary mixtures of particles with improved accuracy. A new model for predicting the void fraction is presented. This model is non-linear and continuous, and it is developed by introducing a packing factor and establishing a mass balance between the solid phases in the packing environment. The results show that the model can accurately predict the void fraction of a binary mixture where the particles are well mixed, partially mixed or segregated. Using this void fraction model and the Ergun equation of pressure drop, the minimum fluidization velocity can be predicted with mean errors of 15.2% for a mixture of two inert materials and 7.0% for a mixture of biomass and inert particles.
dc.language.isoeng
dc.titlePrediction of void fraction and minimum fluidization velocity of a binary mixture of particles: Bed material and fuel particles
dc.typePeer reviewed
dc.typeJournal article
dc.description.versionpublishedVersion
dc.source.pagenumber99-107
dc.source.volume349
dc.source.journalPowder Technology
dc.identifier.doi10.1016/j.powtec.2019.03.027
dc.identifier.cristin1709618
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode1


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