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dc.contributor.authorEchevarría Díez-Canedo, Carlos
dc.contributor.authorValderrama Ángel, César Alberto
dc.contributor.authorCortina Pallás, José Luís
dc.contributor.authorArnaldos, Marina
dc.contributor.authorBernat Camí, Xavier
dc.contributor.authorDe la Cal, Agustina
dc.contributor.authorBoleda, Maria Rosa
dc.contributor.authorVega, Àlex
dc.contributor.authorTeuler, Albert
dc.contributor.authorCastellví, E.
dc.contributor.otherUniversitat Politècnica de Catalunya. Doctorat en Enginyeria de Processos Químics
dc.contributor.otherUniversitat Politècnica de Catalunya. Departament d'Enginyeria Química
dc.date.accessioned2020-11-20T13:59:21Z
dc.date.available2022-11-11T01:28:03Z
dc.date.issued2020-11-10
dc.identifier.citationEchevarría, C. [et al.]. Hybrid sorption and pressure-driven membrane technologies for organic micropollutants removal in advanced water reclamation: A techno-economic assessment. "Journal of cleaner production", 10 Novembre 2020, vol. 273, p. 123108:1-123108:12.
dc.identifier.issn0959-6526
dc.identifier.urihttp://hdl.handle.net/2117/332725
dc.description.abstractThe persistence of certain organic-micropollutants (OMP) in conventional wastewater and reclamation treatments represents a growing concern due to its associated uncertain effects on human health and the environment. This issue highlights the need to resort to advanced treatment technologies to ensure the maximum removal of these compounds. A prototype (1.5–2 m3/h) based on the combination of powdered activated carbon (PAC) with tight ultrafiltration (UF) membranes was operated in El Baix Llobregat Water Reclamation Plant (WRP) for 18 months. Its performance was compared from a technical and economic point of view with the current full-scale ultrafiltration and reverse osmosis system (UF-RO with 50% blend). The application of a PAC concentration of 20 mg/L and its separation with UF membrane resulted in an average removal up to 81 ± 13% of the most recalcitrant OMP detected (Carbamazepine (CBZ), Diuron (DIU), Diclofenac (DCF), Erythromycin (ERY) and Sulphametoxazole (SMX)), while in UF-RO (50% blend), the average removal was 55 ± 11%. PAC-tight UF presented promising advantages for when these post-treatments need to be implemented in inland WRP and where brine management can represent a drawback. Moreover, PAC-tight UF presents 22% higher Operational Expenditures (OPEX) than UF-RO (50% blend), although in terms of Capital Expenditure (CAPEX), it appears as the less expensive option.
dc.language.isoeng
dc.rightsAttribution-NonCommercial-NoDerivs 3.0 Spain
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/3.0/es/
dc.subjectÀrees temàtiques de la UPC::Enginyeria química::Indústria dels processos químics
dc.subject.lcshChemical processes
dc.subject.lcshWater -- Purification
dc.subject.otherOrganic-micropollutants
dc.subject.otherWater reclamation
dc.subject.otherHybrid systems
dc.subject.otherPowdered activated carbon
dc.subject.otherUltrafiltration
dc.subject.otherReverse osmosis
dc.titleHybrid sorption and pressure-driven membrane technologies for organic micropollutants removal in advanced water reclamation: A techno-economic assessment
dc.typeArticle
dc.subject.lemacOsmosi inversa
dc.subject.lemacProcessos químics
dc.subject.lemacAigua -- Depuració
dc.contributor.groupUniversitat Politècnica de Catalunya. R2EM - Resource Recovery and Environmental Management
dc.identifier.doi10.1016/j.jclepro.2020.123108
dc.description.peerreviewedPeer Reviewed
dc.relation.publisherversionhttps://www.sciencedirect.com/science/article/abs/pii/S095965262033153X
dc.rights.accessOpen Access
local.identifier.drac29435090
dc.description.versionPostprint (author's final draft)
local.citation.authorEchevarría, C.; Valderrama, C.; Cortina, J.; Arnaldos, M.; Bernat, X.; De la Cal, A.; Boleda, M.; Vega, À.; Teuler, A.; Castellví, E.
local.citation.publicationNameJournal of cleaner production
local.citation.volume273
local.citation.startingPage123108:1
local.citation.endingPage123108:12


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