Please use this identifier to cite or link to this item: http://nopr.niscpr.res.in/handle/123456789/16874
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dc.contributor.authorChelliapan, S.-
dc.contributor.authorSallis, P.J.-
dc.date.accessioned2013-04-13T10:18:41Z-
dc.date.available2013-04-13T10:18:41Z-
dc.date.issued2013-04-
dc.identifier.issn0975-1084 (Online); 0022-4456 (Print)-
dc.identifier.urihttp://hdl.handle.net/123456789/16874-
dc.description248-254en_US
dc.description.abstractFurther polishing of effluent (pharmaceutical wastewater) from an aerobic reactor using different types of advanced oxidation processes (AOPs) were presented and discussed. Four types of processes were evaluated, i.e. ozonation (O3), hydrogen peroxide (H2O2), ultraviolet (UV) and Fenton reagent, and a combination of these AOPs (O3/UV, H2O2/UV, O3/H2O2 and O3/H2O2/UV) for organic compound (as chemical oxygen demand, COD) removal have also been studied. The additional treatment of the activated sludge reactor effluent contributed substantially to overall COD removal of the pharmaceutical wastewater. Among the AOPs used in this study, O3/H2O2/UV alternative resulted in the highest COD removal (59%) from the activated sludge effluent. In specific, around 450 mg.L-1 of COD had been removed in the O3/H2O2/UV process giving a final COD of 300 mg.L-1 in the treated effluent. Other processes (Fenton, O3, O3/UV, O3/H2O2 and H2O2/UV) showed nearly constant maximum removal of 38 – 43%.en_US
dc.language.isoen_USen_US
dc.publisherNISCAIR-CSIR, Indiaen_US
dc.rights CC Attribution-Noncommercial-No Derivative Works 2.5 Indiaen_US
dc.sourceJSIR Vol.72(04) [April 2013]en_US
dc.subjectAdvanced oxidation processes (AOPs)en_US
dc.subjectPharmaceutical wastewateren_US
dc.subjectOzonationen_US
dc.subjectHydrogen peroxideen_US
dc.subjectUltravioleten_US
dc.subjectFenton reagenten_US
dc.titleRemoval of organic compound from pharmaceutical wastewater using advanced oxidation processesen_US
dc.typeArticleen_US
Appears in Collections:JSIR Vol.72(04) [April 2013]

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