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dc.contributor.authorPěnička , Michal
dc.contributor.authorHoffman , Pavel
dc.contributor.authorFořt , Ivan
dc.date.accessioned2017-02-09T09:27:01Z
dc.date.available2017-02-09T09:27:01Z
dc.date.issued2014
dc.identifier.citationActa Polytechnica. 2014, vol. 54, no. 3, p. 231-239.
dc.identifier.issn1210-2709 (print)
dc.identifier.issn1805-2363 (online)
dc.identifier.urihttp://hdl.handle.net/10467/67132
dc.description.abstractThis article describes intensification of the fluidized-bed drying process for regenerated spherical-shape ion exchanger particles in the batch mode, achieved by a mechanical stirrer in the fluidized bed layer of the dried particles. The effect of the mechanical stirring system on the drying process was examined. Calculations as well as results of comparison measurements provide evidence of a favourable effect of stirring on the total drying time as compared to the initial unstirred system. The regenerated ion exchanger particles pass to the fluid state in a shorter time and the ultimate total drying time is thus more than 60% shorter.en
dc.format.mimetypeapplication/pdf
dc.language.isoeng
dc.publisherČeské vysoké učení technické v Prazecs
dc.publisherCzech Technical University in Pragueen
dc.relation.ispartofseriesActa Polytechnica
dc.relation.urihttps://ojs.cvut.cz/ojs/index.php/ap/article/view/2035
dc.rightsCreative Commons Attribution 4.0 International Licenseen
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/
dc.titleSTIRRED FLUIDIZED-BED DRYER OF REGENERATED ION EXCHANGER PARTICLES
dc.typearticleen
dc.date.updated2017-02-09T09:27:01Z
dc.identifier.doi10.14311/AP.2014.54.0231
dc.rights.accessopenAccess
dc.type.statusPeer-reviewed
dc.type.versionpublishedVersion


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Zobrazit minimální záznam

Creative Commons Attribution 4.0 International License
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