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dc.contributor.authorWang, Chih-Chengen_US
dc.contributor.authorKumar, Mathavaen_US
dc.contributor.authorLan, Chien-Juen_US
dc.contributor.authorLin, Jih-Gawen_US
dc.date.accessioned2014-12-08T15:20:52Z-
dc.date.available2014-12-08T15:20:52Z-
dc.date.issued2011-08-01en_US
dc.identifier.issn1944-3994en_US
dc.identifier.urihttp://dx.doi.org/10.5004/dwt.2011.2175en_US
dc.identifier.urihttp://hdl.handle.net/11536/14851-
dc.description.abstractSimultaneous partial nitrification, anammox and denitrification (SNAD) process was developed in a sequential batch reactor (SBR), and the application of SNAD process for landfill-leachate treatment was investigated. The SNAD process was developed from the biomass of a full-scale landfill-leachate treatment plant. After the adaptation of biomass, the SBR was operated in four stages (I-IV) with varying nitrogen loading rates (NLRs), i.e. 118-280 mg-N/L/d, and organic loading rates (OLRs), i.e. 100-200 mg/L/d. The increase in the NLR has proportionately reduced the NH(4)(+)-N removal. However, the NO(2)(-)-N concentration was close to zero and the NO(3)(-)-N concentration was less than 36 mg/L in all the stages. A consistent chemical oxygen demand (COD) removal was observed in stages I to IV, which indicate that the SBR was not affected by the increase or decrease of the OLR. The total nitrogen removal in the SBR was mainly achieved by partial nitrification and anammox (69-88%) that was evaluated by a stoichiometric model. Moreover, the influence of NLR and OLR on the SNAD process was determined based on sensitivity index (SI). The SI values indicate that the SNAD process was highly affected by the influent NH(4)(+)-N compared to COD.en_US
dc.language.isoen_USen_US
dc.subjectNitrificationen_US
dc.subjectDenitrificationen_US
dc.subjectAnammoxen_US
dc.subjectSequential batch reactoren_US
dc.subjectLandfill-leachateen_US
dc.titleLandfill-leachate treatment by simultaneous partial nitrification, anammox and denitrification (SNAD) processen_US
dc.typeArticle; Proceedings Paperen_US
dc.identifier.doi10.5004/dwt.2011.2175en_US
dc.identifier.journalDESALINATION AND WATER TREATMENTen_US
dc.citation.volume32en_US
dc.citation.issue1-3en_US
dc.citation.spage4en_US
dc.citation.epage9en_US
dc.contributor.department環境工程研究所zh_TW
dc.contributor.departmentInstitute of Environmental Engineeringen_US
dc.identifier.wosnumberWOS:000297923600002-
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