Three-Dimensional Computational Fluid Dynamics (CFD) Study of the Gas-Particle Circulation Pattern Within a Fluidized Bed Granulator: By Full-Factorial Design of Fluidization Velocity and Particle Size

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dc.cclicenceCC-BY-NCen
dc.contributor.authorLiu, Huolongen
dc.contributor.authorYoon, S.en
dc.contributor.authorLi, M.en
dc.date.accessioned2016-10-13T13:47:32Z
dc.date.available2016-10-13T13:47:32Z
dc.date.issued2016-10-04
dc.descriptionThis is the authors accepted manuscripten
dc.fundern/aen
dc.identifier.citationLiu, H., Yoon, S. and Li, M. (2016) Three-Dimensional Computational Fluid Dynamics (CFD) Study of the Gas-Particle Circulation Pattern Within a Fluidized Bed Granulator: By Full-Factorial Design of Fluidization Velocity and Particle Size. Drying Technology, 35 (9), pp. 1043-1058en
dc.identifier.doihttps://doi.org/10.1080/07373937.2016.1230628
dc.identifier.urihttp://hdl.handle.net/2086/12677
dc.language.isoenen
dc.peerreviewedYesen
dc.projectidn/aen
dc.publisherTaylor and Francisen
dc.researchinstituteLeicester Institute for Pharmaceutical Innovation - From Molecules to Practice (LIPI)en
dc.titleThree-Dimensional Computational Fluid Dynamics (CFD) Study of the Gas-Particle Circulation Pattern Within a Fluidized Bed Granulator: By Full-Factorial Design of Fluidization Velocity and Particle Sizeen
dc.typeArticleen

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