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dc.contributor.authorRamakrishna, Elagonda-
dc.date.accessioned2014-12-03T08:16:26Z-
dc.date.available2014-12-03T08:16:26Z-
dc.date.issued2007-
dc.identifierM.Techen_US
dc.identifier.urihttp://hdl.handle.net/123456789/12865-
dc.guideKumar, Surendar-
dc.guideSingh, Shishir-
dc.description.abstractIn today's scenario of pollution world there is a need to produce fuels which do less pollution like Hydrogen. Methane reforming in membrane reactor is one of the processes to produce ultra pure hydrogen (99.999%). Today it is one of the fields in which many researchers are paying attention to. In my present work, model equations for Steam reforming of methane in a Pd/SS membrane reactor based on axial dispersion model an PFR assumptions are developed. Model equations are developed for key components and solved them through MATLAB 7. Various parameters affecting the conversions of CH4, CO2, and permeation of I-I2 are calculated for a wide range of their availability. After the study it is always recommended that care has to be taken while designing process strategy as temperature and steam to methane ratio are affecting greatly the conversion. And it is also recommended to conduct this Reaction. Scheme in a membrane reactor which can perform close to Ideal reactor modelen_US
dc.language.isoenen_US
dc.subjectCHEMICAL ENGINEERINGen_US
dc.subjectSTEAM REFORMINGen_US
dc.subjectMETHANEen_US
dc.subjectMEMBRANE REACTORen_US
dc.titleSTEAM 'REFORMING OF METHANE IN A MEMBRANE REACTORen_US
dc.typeM.Tech Dessertationen_US
dc.accession.numberG13250en_US
Appears in Collections:MASTERS' THESES (Chemical Engg)

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