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Experimental Investigation of Radial Gas Dispersion Coefficients in a Fluidized Bed



dc.contributor.authorŠtefanica , Jiří
dc.contributor.authorHrdlička , Jan
dc.date.accessioned2017-02-08T11:54:57Z
dc.date.available2017-02-08T11:54:57Z
dc.date.issued2012
dc.identifier.citationActa Polytechnica. 2012, vol. 52, no. 3.
dc.identifier.issn1210-2709 (print)
dc.identifier.issn1805-2363 (online)
dc.identifier.urihttp://hdl.handle.net/10467/66947
dc.description.abstractIn a fluidized bed boiler, the combustion efficiency, the NOX formation rate, flue gas desulphurization and fluidized bed heat transfer are all ruled by the gas distribution. In this investigation, the tracer gas method is used for evaluating the radial gas dispersion coefficient. CO2 is used as a tracer gas, and the experiment is carried out in a bubbling fluidized bed cold model. Ceramic balls are used as the bed material. The effect of gas velocity, radial position and bed height is investigated.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/1568
dc.rightsCreative Commons Attribution 4.0 International Licenseen
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/
dc.subjectfluidized beden
dc.subjectgas mixingen
dc.subjectradial dispersionen
dc.titleExperimental Investigation of Radial Gas Dispersion Coefficients in a Fluidized Bed
dc.typearticleen
dc.date.updated2017-02-08T11:54:58Z
dc.rights.accessopenAccess
dc.type.statusPeer-reviewed
dc.type.versionpublishedVersion


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Creative Commons Attribution 4.0 International License
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