Please use this identifier to cite or link to this item: http://hdl.handle.net/10773/26095
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dc.contributor.authorJaria, Guilainept_PT
dc.contributor.authorCalisto, Vâniapt_PT
dc.contributor.authorSilva, Carla Patríciapt_PT
dc.contributor.authorGil, María Victoriapt_PT
dc.contributor.authorOtero, Martapt_PT
dc.contributor.authorEsteves, Valdemar I.pt_PT
dc.date.accessioned2019-05-23T14:17:52Z-
dc.date.issued2019-
dc.identifier.issn0048-9697pt_PT
dc.identifier.urihttp://hdl.handle.net/10773/26095-
dc.description.abstractThis work aimed to assess the fixed-bed adsorptive performance of a primary paper mill sludge-based granular activated carbon (PSA-PA) for the removal of pharmaceuticals, namely carbamazepine (CBZ), sulfamethoxazole (SMX) and paroxetine (PAR), from water. The breakthrough curves corresponding to the adsorption of CBZ at different flow rates and in two different matrices (distilled and urban wastewater) were firstly determined, which allowed to select the most favorable flow rate for the subsequent experiments. The fixed-bed adsorption of CBZ, SMX and PAR from single and ternary solutions in wastewater showed that the performance of PSA-PA was different for each pharmaceutical. According to the obtained breakthrough curves, the poorest bed adsorption capacity, either from single or ternary solution, was that for SMX, which may be related with electrostatic repulsion at the pH of the wastewater used (pH ~ 7.3–7.7). Also, the bed adsorption capacity of PSA-PA for SMX was notoriously lower in the ternary than in the single solution, while it slightly decreased for CBZ and even increased for PAR. The regeneration studies showed that the CBZ adsorption capacity of the PSA-PA bed decreased about 38 and 71% after the first and the second thermal regeneration stages, respectively. This decline was comparatively larger than the corresponding reduction of the PSA-PA specific surface area (SBET), which decreased only 5 and 25% for the first and second regeneration, respectively, and pointed to the lack of viability of more than one regeneration stage.pt_PT
dc.language.isoengpt_PT
dc.publisherElsevierpt_PT
dc.relationPTDC/AAG-TEC/1762/2014pt_PT
dc.relationUID/AMB/50017/2019pt_PT
dc.relationinfo:eu-repo/grantAgreement/FCT/SFRH/SFRH%2FBPD%2F78645%2F2011/PTpt_PT
dc.relationSFRH/BD/138388/2018pt_PT
dc.relationIF/00314/2015pt_PT
dc.relationCEECIND/00007/2017pt_PT
dc.rightsopenAccesspt_PT
dc.rights.urihttps://creativecommons.org/licenses/by/4.0/pt_PT
dc.subjectColumn reactorpt_PT
dc.subjectPharmaceuticalspt_PT
dc.subjectMulticomponent adsorptionpt_PT
dc.subjectBreakthrough curvept_PT
dc.subjectThermal regenerationpt_PT
dc.titleFixed-bed performance of a waste-derived granular activated carbon for the removal of micropollutants from municipal wastewaterpt_PT
dc.typearticlept_PT
dc.description.versionpublishedpt_PT
dc.peerreviewedyespt_PT
degois.publication.titleScience of The Total Environmentpt_PT
dc.date.embargo2021-06-01-
dc.relation.publisherversionhttps://www.sciencedirect.com/science/article/pii/S0048969719322375pt_PT
dc.identifier.doi10.1016/j.scitotenv.2019.05.198pt_PT
dc.identifier.essn1879-1026pt_PT
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