Heterotrophic-autotrophic sequential system for reductive nitrate and perchlorate removal

dc.authorid0000-0002-9898-9173
dc.authorid0000-0002-0536-6250
dc.authorid0000-0002-4904-6056
dc.contributor.authorUçar, Deniz
dc.contributor.authorCokgor, Emine Ubay
dc.contributor.authorŞahinkaya, Erkan
dc.date.accessioned2025-05-10T19:45:05Z
dc.date.issued2016
dc.departmentİMÜ, Fakülteler, Mühendislik ve Doğa Bilimleri Fakültesi, Biyomühendislik Bölümü
dc.description.abstractNitrate and perchlorate were identified as significant water contaminants all over the world. This study aims at evaluating the performances of the heterotrophic-autotrophic sequential denitrification process for reductive nitrate and perchlorate removal from drinking water. The reduced nitrate concentration in the heterotrophic reactor increased with increasing methanol concentrations and the remaining nitrate/nitrite was further removed in the following autotrophic denitrifying process. The performances of the sequential process were studied under varying nitrate loads of 0.6 -1.2 g NO3- -N/(Ld) at a fixed hydraulic retention time of 2 h. The C/N ratio in the heterotrophic reactor varied between 1.24 and 2.77 throughout the study. Nitrate and perchlorate reduced completely with maximum initial concentrations of 100 mg NO3 -N/L and 1000 mu g/L, respectively. The maximum denitrification rate for the heterotrophic reactor was 2.4 g NO3 -N/(Ld) when the bioreactor was fed with 100 mgNO(3)(-)-N/L and 277 mg/L methanol. For the autotrophic reactor, the highest denitrification rate was 0.86 mgNO(3)(-)-N/(Ld) in the first period when the heterotrophic reactor performance was low. Perchlorate reduction was initiated in the heterotrophic reactor, but completed in the following autotrophic process. Effluent sulphate concentration was below the drinking water standard level of 250 mg/L and pH was in the neutral level.
dc.description.sponsorshipScientific and Technological Research Council of Turkey [113Y023]
dc.description.sponsorshipThis work was supported by The Scientific and Technological Research Council of Turkey under project no. 113Y023.
dc.identifier.doi10.1080/09593330.2015.1065009
dc.identifier.endpage191
dc.identifier.issn0959-3330
dc.identifier.issn1479-487X
dc.identifier.issue2
dc.identifier.pmid26102288
dc.identifier.scopus2-s2.0-84948584196
dc.identifier.scopusqualityQ1
dc.identifier.startpage183
dc.identifier.urihttps://doi.org/10.1080/09593330.2015.1065009
dc.identifier.urihttps://hdl.handle.net/20.500.14730/11147
dc.identifier.volume37
dc.identifier.wosWOS:000365600000004
dc.identifier.wosqualityQ3
dc.indekslendigikaynakWeb of Science
dc.indekslendigikaynakScopus
dc.indekslendigikaynakPubMed
dc.language.isoen
dc.publisherTaylor & Francis Ltd
dc.relation.ispartofEnvironmental Technology
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı
dc.rightsinfo:eu-repo/semantics/closedAccess
dc.snmzKA_WOS_20250302
dc.subjectnitrate reduction
dc.subjectperchlorate reduction
dc.subjectsequential system
dc.subjectelemental sulphur
dc.subjectheterotrophic process
dc.titleHeterotrophic-autotrophic sequential system for reductive nitrate and perchlorate removal
dc.typeArticle

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