Integrated renewable H2 production and industrial wastewater treatment using a semi-pilot scale flow electrolyzer

dc.citation.volume507
dc.contributor.authorSgarbi, Ricardo
dc.contributor.authorMandelli, Cecília Montanha
dc.contributor.authorRuotolo, Luís Augusto Martins
dc.contributor.authorlatteshttp://lattes.cnpq.br/2388966785886132
dc.contributor.authorlatteshttp://lattes.cnpq.br/6167735734348703
dc.contributor.authorlatteshttp://lattes.cnpq.br/5876631381345673
dc.contributor.authororcidhttps://orcid.org/0000-0002-1337-9596
dc.contributor.authororcidhttps://orcid.org/0000-0003-2517-0017
dc.coverage.spatialOnline
dc.date.accessioned2025-05-20T17:27:16Z
dc.date.issued2025-03-01
dc.description.abstractIntegration of mandatory wastewater treatment with renewable H2 production has been explored as a cost-reduction strategy, by trading the generated H2 as feedstock to relevant industries. A semi-pilot scale flow electrolyzer, innovatively designed for this purpose, demonstrated promising performance. Both the cathodic hydrogen evolution reaction and the anodic organic electrooxidation were investigated under two sets of operational conditions: (i) temperature, current density, and conductivity, and (ii) membrane type, and catholyte concentration. Thereupon, it is observed that a highly conductive, alkalinized catholyte, in combination with a low-cost anion exchange membrane, enhances both reactions by amplifying conductivity, promoting OH– ion transport, and accelerating anode kinetics. Furthermore, the electrolyzer successfully treated industrial wastewater while simultaneously producing renewable H2 with low CO2 emissions: 2.0 kgCO2 kgH2-1. The overall process cost was mainly influenced by electricity prices, ranging from 2.7 to 15.7 US$ kgH2-1 under optimized conditions.eng
dc.description.sponsorshipConselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)
dc.description.sponsorshipFundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)
dc.description.sponsorshipIdFAPESP 2022/12895-1
dc.description.sponsorshipIdFAPESP 2023/06600-1
dc.description.sponsorshipIdCNPq 406156/2022-0
dc.description.sponsorshipIdCNPq 351865/2023-3
dc.description.sponsorshipIdFAPESP 2024/11001-2
dc.description.sponsorshipIdCNPq PIBIC1331
dc.format.extent160547
dc.identifierhttps://doi.org/10.1016/j.cej.2025.160547
dc.identifier.citationSGARBI, Ricardo; MANDELLI, Cecília Montanha; RUOTOLO, Luís Augusto Martins. Integrated renewable H2 production and industrial wastewater treatment using a semi-pilot scale flow electrolyzer. Chemical Engineering Journal, Online, v. 507, p. 160547, 2025. Disponível em: https://repositorio.ufscar.br/handle/20.500.14289/22089.por
dc.identifier.issn1873-3212
dc.identifier.issn1385-8947
dc.identifier.urihttps://hdl.handle.net/20.500.14289/22089
dc.identifier.urlhttps://www.sciencedirect.com/science/article/pii/S1385894725013683?via%3Dihub
dc.language.isoeng
dc.publisherUniversidade Federal de São Carlos
dc.publisher.addressCampus São Carlos
dc.publisher.centerCentro de Ciências Exatas e de Tecnologia - CCET
dc.publisher.departmentDepartamento de Engenharia Química - DEQ
dc.publisher.initialsUFSCar
dc.publisher.programPrograma de Pós-Graduação em Engenharia Química - PPGEQ
dc.relation.ispartofChemical Engineering Journal
dc.rightsAttribution-NonCommercial-NoDerivs 3.0 Brazilen
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/3.0/br/
dc.subjectGreen hydrogen productioneng
dc.subjectElectrochemical reactoreng
dc.subjectKineticseng
dc.subjectPhenol electrooxidationeng
dc.subjectReal effluenteng
dc.subject.cnpqENGENHARIAS::ENGENHARIA QUIMICA::TECNOLOGIA QUIMICA
dc.titleIntegrated renewable H2 production and industrial wastewater treatment using a semi-pilot scale flow electrolyzereng
dc.typeArtigo
dc.versiontypepós-print do autor

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