Please use this identifier to cite or link to this item: http://nopr.niscpr.res.in/handle/123456789/33812
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dc.contributor.authorAhmad, Anwar-
dc.date.accessioned2016-02-24T09:13:22Z-
dc.date.available2016-02-24T09:13:22Z-
dc.date.issued2016-01-
dc.identifier.issn0975-0991 (Online); 0971-457X (Print)-
dc.identifier.urihttp://hdl.handle.net/123456789/33812-
dc.description31-38en_US
dc.description.abstractAnaerobic digestion of palm oil mill effluent (POME) for continuous biogas production has been carried out in an upflow anaerobic sludge blanket reactor (UASBR) using cement kiln dust (CKD). POME is used as the substrate carbon source and CKD as a neutralizing agent. The effects of the hydrualic retention time (HRT) 20 h and organic loading rate (OLR) 4.5 kg COD/m3h-1 over 95% COD removal and 0.89 mL CH4/L/h with a methane yield of 0.65 L CH4/g CODremoved  at 1600 mg/L CKD in UASBR have been studied. Without CKD (control) the reactor for the removal of COD only 10.5% and methane production up to 0.13 L CH4/g COD. However, increasing the OLR to 4.5 kgCOD/m3h-1 by reducing the hydraulic retention time (HRT 6 h) reduced the COD removal efficiency to 58% and methane production up to 0.43 L CH4/g CODremoved. Considering this, the use of CKD containing UASBR might be practically and economically attractive for industrial scale biogas production and sludge reduction from industrial wastes and wastewater. 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.sourceIJCT Vol.23(1) [January 2016]en_US
dc.subjectCement kiln dusten_US
dc.subjectMethaneen_US
dc.subjectOrganic loading rateen_US
dc.subjectHydraulic retention timeen_US
dc.subjectSolid sludge removalen_US
dc.titleApplication of cement kiln dust enhancing methane production using upflow anaerobic sludge blanket reactor for the treatment of palm oil mill effluenten_US
dc.typeArticleen_US
Appears in Collections:IJCT Vol.23(1) [January 2016]

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