Utilize este identificador para referenciar este registo: https://hdl.handle.net/10216/120269
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Campo DCValorIdioma
dc.creatorAmorim C.L.
dc.creatorMoreira I.S.
dc.creatorRibeiro A.R.
dc.creatorSantos L.H.M.L.M.
dc.creatorDelerue-Matos C.
dc.creatorTiritan M.E.
dc.creatorCastro P.M.L.
dc.date.accessioned2019-05-31T16:14:19Z-
dc.date.available2019-05-31T16:14:19Z-
dc.date.issued2016
dc.identifier.issn09648305
dc.identifier.urihttps://hdl.handle.net/10216/120269-
dc.description.abstractAn aerobic granular sludge-sequencing batch reactor (AGS-SBR) was fed for 28-days with a simulated wastewater containing a mixture of chiral pharmaceuticals (CPs) (alprenolol, bisoprolol, metoprolol, propranolol, venlafaxine, salbutamol, fluoxetine and norfluoxetine), each at 1.3 μg L−1. AGS-SBR exhibited the highest removal efficiency for norfluoxetine, with preferential removal of the (R)-enantiomer indicating that biological-mediated processes occurred. For all other CPs, removal was non-enantioselective, occurring through biosorption onto AGS. A gradual decline of CPs removal was observed, probably related to the decrease of AGS adsorption capacity. Moreover, chemical oxygen demand (COD) content in the bulk liquid after anaerobic feeding increased, and P-release dropped, probably because the polyphosphate-accumulating organism's activity was affected. Nitrification was also affected as indicated by the ammonium effluent concentration increase. Moreover, CPs exposure promoted AGS disintegration, with decreasing granule size. After stopping CPs feeding, the AGS started to recover its compact structure, and the system returned its normal performance concerning COD- and P-removal. N-removal seemed to be a more sensitive process, as while the ammonium levels were fully restored at the end of operation, nitrite reduction was only partially restored. Results provide useful information on AGS performance during the treatment of wastewater containing pharmaceuticals, a frequent scenario in WWTP. © 2016
dc.description.sponsorshipC.L. Amorim, I.S. Moreira and A.R. Ribeiro acknowledge research grants from Fundação para a Ciência e Tecnologia (FCT), Portugal (SFRH/BPD/96481/2013, SFRH/BPD/87251/2012 and SFRH/BD/64999/2009) and Fundo Social Europeu (Programa Operacional Potencial Humano (POPH), Quadro de Referência Estratégico Nacional (QREN)). This work was supported by FCT through the projects PTDC/EBB-EBI/111699/2009, UID/Multi/50016/2013, UID/Multi/04423/2013 and UID/QUI/50006/2013. This work also received financial support from the European Regional Development Fund through COMPETE – and PHARMADRUGS-CESPU 2014. Operational Competitiveness Programme. The authors also thank to COST Action ES1202: Conceiving Wastewater Treatment in 2020 - Energetic, environmental and economic challenges. Thanks to Dr R.C. Pullar for corrections to the English.
dc.language.isoeng
dc.publisherElsevier
dc.relationinfo:eu-repo/grantAgreement/FCT/5876/147268/PT
dc.relation.ispartofInternational Biodeterioration and Biodegradation, vol. 115, p. 277-285
dc.rightsrestrictedAccess
dc.subjectBacteria
dc.subjectBatch reactors
dc.subjectChemical oxygen demand
dc.subjectDrug products
dc.subjectEffluents
dc.subjectEnantiomers
dc.subjectGranular materials
dc.subjectMixtures
dc.subjectRestoration
dc.subjectStereochemistry
dc.subjectAdsorption capacities
dc.subjectAerobic granular sludges
dc.subjectChiral pharmaceuticals
dc.subjectEffluent concentrations
dc.subjectGranular morphology
dc.subjectNutrients removal
dc.subjectPolyphosphate-accumulating organisms
dc.subjectRemoval efficiencies
dc.subjectWastewater treatment
dc.titleTreatment of a simulated wastewater amended with a chiral pharmaceuticals mixture by an aerobic granular sludge sequencing batch reactor
dc.typeArtigo em Revista Científica Internacional
dc.contributor.uportoCIIMAR - Centro Interdisciplinar de Investigação Marinha e Ambiental
dc.identifier.doi10.1016/j.ibiod.2016.09.009
dc.relation.publisherversionhttp://dx.doi.org/10.1016/j.ibiod.2016.09.009
Aparece nas coleções:CIIMAR - Artigo em Revista Científica Internacional

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