Please use this identifier to cite or link to this item: http://nopr.niscair.res.in/handle/123456789/1119
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dc.contributor.authorUzun, Değer-
dc.contributor.authorGülfen, Mustafa-
dc.date.accessioned2008-04-23T05:40:51Z-
dc.date.available2008-04-23T05:40:51Z-
dc.date.issued2007-05-
dc.identifier.issn0971–457X-
dc.identifier.urihttp://hdl.handle.net/123456789/1119-
dc.description263-268en_US
dc.description.abstractDissolution kinetics for the removals of iron and aluminium from red mud, a by-product or waste of the Bayer Process, with sulphuric acid were studied. The process parameters studied include calcination temperature, sulphuric acid concentration, particle size, agitation rate, dissolution temperature and time. Temperature and acid concentration had strong influence on the dissolution of iron and aluminium. The mechanism for the dissolution of both iron and aluminium followed first order kinetic model equation (F1), -ln(1-α) = kt, controlled by interfacial chemical reaction, with the apparent activation energies of 61.42 and 7.39 kJ/mol, respectively. Using 6 M acid, the removals of 97.46% iron and 64.40% aluminium were achieved from red mud calcined at 873 K.en_US
dc.language.isoen_USen_US
dc.publisherCSIRen_US
dc.relation.ispartofseriesC22B3/00en_US
dc.sourceIJCT Vol.14(3) [May 2007]en_US
dc.subjectDissolution kineticsen_US
dc.subjectRed muden_US
dc.subjectIronen_US
dc.subjectAluminiumen_US
dc.subjectSulphuric aciden_US
dc.titleDissolution kinetics of iron and aluminium from red mud in sulphuric acid solutionen_US
dc.typeArticleen_US
Appears in Collections:IJCT Vol.14(3) [May 2007]

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