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dc.contributor.authorChen, W. H.en_US
dc.contributor.authorChiang, Y. A.en_US
dc.contributor.authorHuang, Y. T.en_US
dc.contributor.authorChen, S. Y.en_US
dc.contributor.authorSung, S.en_US
dc.contributor.authorLin, J. G.en_US
dc.date.accessioned2018-08-21T05:54:00Z-
dc.date.available2018-08-21T05:54:00Z-
dc.date.issued2017-05-01en_US
dc.identifier.issn0964-8305en_US
dc.identifier.urihttp://dx.doi.org/10.1016/j.ibiod.2017.01.037en_US
dc.identifier.urihttp://hdl.handle.net/11536/145469-
dc.description.abstractThe study aimed to polish wastewater effluent from an activated treatment system for nitrogen removal by a packed bed bioreactor (PBR). The nitrogen removal via simultaneous partial nitrification, anammox and denitrification (SNAD) process was investigated with different hydraulic retention times (HRTs). The results show that both effluent ammonia-and nitrate-nitrogen concentrations approached to 0 mg/L at the HRT as low as 3 h. The total nitrogen removal efficiency decreased from an average of 84% at both 18- and 24-h HRTs to 38% at 3-h HRT. This low nitrogen removal efficiency was due to the presence of incomplete degradation of organic nitrogen at shorter HRTs. The analysis using quantitative real-time polymerase chain reaction resolves that the ratio of ammonia-oxidizing bacteria (AOB) to the domain Eubacteria changed limited in the range between 2.8 and 4.0% during the continuous operation. Meanwhile, the nitrite-oxidizing bacteria (NOB) increased from 0.0 to 2.9% when the HRT was gradually reduced to 3 h. The anammox bacteria accounting for 30.5% of microbial consortia dominated the AOB and the NOB at the 3-h HRT. In sum, inorganic form of nitrogen in a typical wastewater plant effluent could be efficiently polished via SNAD process in the PBR. (C) 2017 Elsevier Ltd. All rights reserved.en_US
dc.language.isoen_USen_US
dc.subjectTertiary treatmenten_US
dc.subjectAmmonia-nitrogenen_US
dc.subjectSNADen_US
dc.subjectAnammoxen_US
dc.subjectPacked bed reactoren_US
dc.subjectMunicipal wastewateren_US
dc.titleTertiary nitrogen nitrogen removal using simultaneous partial nitrification, anammox and denitrification (SNAD) process in packed bed reactoren_US
dc.typeArticleen_US
dc.identifier.doi10.1016/j.ibiod.2017.01.037en_US
dc.identifier.journalINTERNATIONAL BIODETERIORATION & BIODEGRADATIONen_US
dc.citation.volume120en_US
dc.citation.spage36en_US
dc.citation.epage42en_US
dc.contributor.department環境工程研究所zh_TW
dc.contributor.departmentInstitute of Environmental Engineeringen_US
dc.identifier.wosnumberWOS:000400716600005en_US
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