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dc.contributor.authorNasr, Somaye
dc.date.accessioned2012-08-30T17:00:06Z
dc.date.available2012-08-30T17:00:06Z
dc.date.issued2012-08-30
dc.identifier.urihttp://hdl.handle.net/10222/15438
dc.description.abstractDue to increasing atmospheric carbon dioxide (CO2) concentration, energy sources that release to the atmosphere smaller amounts of CO2 are of interest. Initially, all the efforts were focused on increasing the system efficiency, now more attention is being paid recently on capturing and sequestering CO2 from combustion process and eliminating discharge to the atmosphere from the major source points. In these circumstances, the chemical-looping combustion (CLC) is a promising concept that can be used in power generation which integrates power production and CO2 capture. The aim of this work is to study reaction kinetics of Chemical-Looping Combustion. In order to come up with a suitable reactor design we should have a good knowledge of the reaction kinetics happening in the air and fuel reactor; then, to get such an information as will be mentioned later, reactivity investigation was carried out in thermogravimetric analysis (TGA).en_US
dc.subjectReaction Kinetics Studiesen_US
dc.titleTHE REDUCTION KINETICS OF IRON OXIDE ORE BY METHANE FOR CHEMICAL-LOOPING COMBUSTIONen_US
dc.typeThesisen_US
dc.date.defence2012-08-16
dc.contributor.departmentDepartment of Process Engineering and Applied Scienceen_US
dc.contributor.degreeMaster of Applied Scienceen_US
dc.contributor.external-examinerDominic Groulxen_US
dc.contributor.graduate-coordinatorGeorge Kipourosen_US
dc.contributor.thesis-readerStephen Kuzaken_US
dc.contributor.thesis-supervisorMicheal J. Pegg, Kevin Plucknetten_US
dc.contributor.ethics-approvalNot Applicableen_US
dc.contributor.manuscriptsNot Applicableen_US
dc.contributor.copyright-releaseNot Applicableen_US
dc.contributor.signature-page-receivedYesen_US
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