Please use this identifier to cite or link to this item: http://localhost:8081/xmlui/handle/123456789/6749
Full metadata record
DC FieldValueLanguage
dc.contributor.authorK., Patel Nilesh-
dc.date.accessioned2014-11-04T08:15:09Z-
dc.date.available2014-11-04T08:15:09Z-
dc.date.issued2002-
dc.identifierM.Techen_US
dc.identifier.urihttp://hdl.handle.net/123456789/6749-
dc.guideKumar, Surendra-
dc.description.abstractThe study of behavior of tubular reactors using ion-exchange resins as catalyst is carried out by making use of a complete two-dimensional heterogeneous model for the reactor, which included the resistance inside the ion-exchange resin particle, considered with a macroreticular structure. The active sites were located inside the gel phase of the resin, represented by microspheres and on the macropores walls. The overall efficiency was defined by two factors one is macro-effectiveness and other is micro-effectiveness. The simulation of methyl tert-butyl ether, MTBE, a liquid phase reversible reaction that is highly exothermic reaction between methanol and iso-butene, was taken into consideration. Heterogeneous model is developed for the synthesis of MTBE in tubular reactor packed with ion-exchange resin, Amberlyst 15. Different model parameters have taken into consideration. Comparison between pseudo homogeneous and heterogeneous model is also done. Effect of wall temperature on axial concentration and axial temperature is also taken into consideration.en_US
dc.language.isoenen_US
dc.subjectCHEMICAL ENGINEERINGen_US
dc.subjectM.TBEen_US
dc.subjectSYNTHESISen_US
dc.subjectTUBULAR REACTOR PACKEDen_US
dc.subjectION EXCHANGE RESINSen_US
dc.titleSIMULATION OF M.TBE (METHYL TERT.BUTYL ETHER) SYNTHESIS IN A TUBULAR REACTOR PACKED WITH ION EXCHANGE RESINSen_US
dc.typeM.Tech Dessertationen_US
dc.accession.numberG10716en_US
Appears in Collections:MASTERS' THESES (Chemical Engg)

Files in This Item:
File Description SizeFormat 
CHD G10710.pdf2.23 MBAdobe PDFView/Open


Items in DSpace are protected by copyright, with all rights reserved, unless otherwise indicated.