Please use this identifier to cite or link to this item: http://nopr.niscair.res.in/handle/123456789/28465
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dc.contributor.authorReddy, P Manoj Kumar-
dc.contributor.authorMahammadunnisa, Sk-
dc.contributor.authorSubrahmanyam, Ch-
dc.date.accessioned2014-04-19T12:23:55Z-
dc.date.available2014-04-19T12:23:55Z-
dc.date.issued2014-04-19T12:23:55Z-
dc.identifier.issn0975-0975(Online); 0376-4710(Print)-
dc.identifier.urihttp://hdl.handle.net/123456789/28465-
dc.description499-503en_US
dc.description.abstractElectrical discharges generated at water-gas interface in a dielectric barrier discharge reactor has been utilized for the degradation and mineralization of a model aqueous organic pollutant, viz., methyl orange. Mineralization of the dye is identified by an online infrared gas analyzer and confirmed by a total organic carbon analyzer. It has been observed that both degradation efficiency and mineralization of the dye increases on addition of modified alumina catalyst to the plasma reactor. On addition of FeOx/Al2O3 catalyst, the mineralization efficiency increases from 31% with plasma reactor alone to 38%. It has been observed that dye degradation followes first-order kinetics and degree of mineralization increases as a function of time with decreasing energy yield. en_US
dc.language.isoen_USen_US
dc.rights CC Attribution-Noncommercial-No Derivative Works 2.5 Indiaen_US
dc.sourceIJC-A Vol.53A(04-05) [April-May 2014]en_US
dc.subjectCatalysten_US
dc.subjectDye degradationen_US
dc.subjectDegradationen_US
dc.subjectDielectric barrier discharge reactoren_US
dc.subjectCatalytic plasma reactoren_US
dc.subjectPlasma reactoren_US
dc.subjectEnergy yielden_US
dc.subjectMineralizationen_US
dc.subjectNonthermal plasmaen_US
dc.subjectTotal organic carbonen_US
dc.subjectMethyl orangeen_US
dc.subjectIron oxideen_US
dc.subjectAluminaen_US
dc.titleMineralization of aqueous organic pollutants using a catalytic plasma reactoren_US
dc.typeArticleen_US
Appears in Collections:IJC-A Vol.53A(04-05) [April-May 2014]

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