Utilize este identificador para referenciar este registo: https://hdl.handle.net/10216/166835
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Campo DCValorIdioma
dc.creatorValenzuela, L
dc.creatorPedrosa, M
dc.creatorBahamonde, A
dc.creatorRosal, R
dc.creatorTorres-Pinto, A
dc.creatorClaudia G Silva
dc.creatorJoaquim Luís Faria
dc.creatorSilva, Adrian
dc.date.accessioned2025-06-02T23:05:37Z-
dc.date.available2025-06-02T23:05:37Z-
dc.date.issued2023
dc.identifier.issn0920-5861
dc.identifier.othersigarra:628945
dc.identifier.urihttps://hdl.handle.net/10216/166835-
dc.description.abstractMetal-free carbon nitride-based membranes were prepared by embedding bulk or exfoliated graphitic carbon nitride (g-C3N4) photocatalysts in a polyvinylidene fluoride (PVDF) matrix. Supported membranes were also fabricated by immobilising these photocatalysts on a polytetrafluoroethylene (PTFE) substrate. The membranes were tested for venlafaxine (VFX) degradation at a feed concentration of 250 mu g L-1 under continuous flow mode operation and using a visible-light emitting diode (LED) as energy source. The reduction of the (002) diffraction peak and the increased intensity of the infrared absorption bands confirmed that the exfoliation process decreased the number of aligned g-C3N4 layers, with a more ordered packing of tri-s-triazine units. Additionally, the small particle size (around 745 and 257 nm for bulk and exfoliated g-C3N4, respectively) and the presence of terminal amino groups in the catalysts allowed for homogeneous dispersion in the PVDF matrix. Despite their different surface roughness and cross-sectional microstructure, all the fabricated membranes exhibited similar photocatalytic filtration performance for VFX degradation, resulting in conversions above 95% after 5 h of irradiation (418 nm with an irradiance of 11.2 W m- 2) and keeping the VFX concentration in the effluent negligible up to 48 h of continuous operation (mass removal rate of about 6 mg m- 2 h-1). In a more complex water matrix (i.e., surface water), the photocatalytic filtration process led to 50% VFX removal (or 3 mg m- 2 h-1) at the steady state. Moreover, the permeate flux remained at about 25 L m- 2 h-1 throughout the continuous operation, suggesting that fouling did not occur at these conditions.
dc.language.isoeng
dc.relationinfo:eu-repo/grantAgreement/Comissão de Coordenação e Desenvolvimento Regional do Norte/P2020|Norte2020-Projetos Integrados ICDT/NORTE-01-0145-FEDER-000069/Healthy Waters - Identification, Elimination, Social Awareness and Education of Water Chemical and Biological Micropollutants with Health and Environmental Implications/Healthy Waters
dc.relationinfo:eu-repo/grantAgreement/FCT - Fundação para a Ciência e a Tecnologia/Programa de Financiamento Plurianual de Unidades de I&D/UIDB/50020/2020_UIDP/50020/2020/Financiamento Plurianual 2020-2023 para a Unidade LA LSRE-LCM Laboratório de Processos de Separação e Reacção - Laboratório de Catálise e Materiais/LA LSRE-LCM
dc.relationinfo:eu-repo/grantAgreement/Comissão de Coordenação e Desenvolvimento Regional do Norte /NORTE2020 - Programa Operacional Regional do Norte 2014/2020/NORTE-01-0145-FEDER-000071/ClimActiC - CidadaniaPeloClima: Criando Pontes entre Cidadania e Ciência para a Adaptação Climática/ClimActiC
dc.rightsrestrictedAccess
dc.titleCarbon nitride-PVDF photocatalytic membranes for visible-light degradation of venlafaxine as emerging water micropollutant
dc.typeArtigo em Revista Científica Internacional
dc.contributor.uportoFaculdade de Engenharia
dc.identifier.doi10.1016/j.cattod.2023.114042
dc.identifier.authenticusP-00Y-66P
Aparece nas coleções:FEUP - Artigo em Revista Científica Internacional

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