Please use this identifier to cite or link to this item: http://nopr.niscpr.res.in/handle/123456789/1272
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dc.contributor.authorKumar, N Senthil-
dc.contributor.authorPalanivelu, K-
dc.date.accessioned2008-05-09T09:20:52Z-
dc.date.available2008-05-09T09:20:52Z-
dc.date.issued2007-06-
dc.identifier.issn0022-4456-
dc.identifier.urihttp://hdl.handle.net/123456789/1272-
dc.description490-494en_US
dc.description.abstractPervaporation (PV), a membrane separation process, has been used to recover from spent solvent of perchloroethylene (PERC), one of the solvents used for surface treatment in electroplating industries. Commercial polydimethylsiloxane (PDMS) flat type membrane (thickness, 200 μm) was employed to remove PERC from spent solvent. A model, based on solutiondiffusion mechanism, was proposed to predict mass transfer during PV. The effects of permeate pressure and feed flow rate on PV were investigated to validate the model. A Pervaporation Separation Index (PSI) of 4198.61 was achieved finally. The moisture content in the final permeate was 1%.en_US
dc.language.isoen_USen_US
dc.publisherCSIRen_US
dc.relation.ispartofseriesB01D61/36en_US
dc.sourceJSIR Vol.66(6) [June 2007]en_US
dc.subjectModellingen_US
dc.subjectPDMSen_US
dc.subjectPerchloroethylenexen_US
dc.subjectPervaporationen_US
dc.subjectSolvent recoveryen_US
dc.titlePervaporative recovery of perchloroethylene from spent solvent of electroplating industry: Experiment and modelling studiesen_US
dc.typeArticleen_US
Appears in Collections:JSIR Vol.66(06) [June 2007]

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