Identificador persistente para citar o vincular este elemento: http://hdl.handle.net/10553/69929
Campo DC Valoridioma
dc.contributor.authorMena, V. F.en_US
dc.contributor.authorBetancor-Abreu, A.en_US
dc.contributor.authorGonzález, S.en_US
dc.contributor.authorDelgado, S.en_US
dc.contributor.authorSouto, R. M.en_US
dc.contributor.authorSantana, J. J.en_US
dc.date.accessioned2020-02-05T12:51:22Z-
dc.date.available2020-02-05T12:51:22Z-
dc.date.issued2019en_US
dc.identifier.issn0301-4797en_US
dc.identifier.otherScopus-
dc.identifier.urihttp://hdl.handle.net/10553/69929-
dc.description.abstractExcessive fluoride content in groundwater can cause serious risks to human health, and sources of groundwater intended for human consumption should be treated to reduce fluoride concentrations down to acceptable levels. In the particular case of the island of Tenerife (Canary Islands, Spain), the water supply comes mainly from aquifers of volcanic origin with a high content of fluorides that make them unacceptable for human consumption without prior conditioning treatment. The treatments that generate a high rejection of water are not acceptable because water is a scarce natural resource of high value. An electrocoagulation process was investigated as a method to treat natural groundwater from volcanic soils containing a hazardously high fluoride content. The operating parameters of an electrocoagulation reactor model with parallel plate aluminum electrodes were optimized for batch and continuous flow operations. In the case of the batch operation, acidification of the water improved the removal efficiency of fluoride, which was the highest at pH 3. However, operation at the natural pH of the water achieved elimination efficiencies between 82 and 92%, depending on the applied current density. An optimum current density of 5 mA/cm2 was found in terms of maximum removal efficiency, and the kinetics of fluoride removal conformed to pseudo-second-order kinetics. In the continuous-flow operation, with the optimal residence time of 10 min and a separation of 0.5 cm between the electrodes, it was observed that the current density that would be applied would depend on the initial concentration of fluoride in the raw water. Thus, an initial fluoride concentration of 6.02 mg/L required a current density >7.5 mA/cm2 to comply with the legal guidelines in the product water, while for an initial concentration of 8.98 mg/L, the optimal current density was 10 mA/cm2. Under these operating conditions, the electrocoagulation process was able to reduce the fluoride concentration of natural groundwater to below 1.5 mg/L according to WHO guidelines with an operating cost between 0.20 and 0.26 €/m3 of treated water.en_US
dc.languageengen_US
dc.relation.ispartofJournal of Environmental Managementen_US
dc.sourceJournal of Environmental Management[ISSN 0301-4797],v. 246, p. 472-483en_US
dc.subject3303 ingeniería y tecnología químicasen_US
dc.subject.otherAluminum Electrodesen_US
dc.subject.otherElectrocoagulation Processen_US
dc.subject.otherFluoride Removalen_US
dc.subject.otherWater Treatmenten_US
dc.titleFluoride removal from natural volcanic underground water by an electrocoagulation process: Parametric and cost evaluationsen_US
dc.typeinfo:eu-repo/semantics/Articleen_US
dc.typeArticleen_US
dc.identifier.doi10.1016/j.jenvman.2019.05.147
dc.identifier.scopus85067033075-
dc.identifier.isi000482246700047
dc.contributor.authorscopusid57201843009-
dc.contributor.authorscopusid56512164300-
dc.contributor.authorscopusid7202200085-
dc.contributor.authorscopusid57197682228-
dc.contributor.authorscopusid7005304036-
dc.contributor.authorscopusid35436067200-
dc.description.lastpage483-
dc.description.firstpage472-
dc.relation.volume246-
dc.investigacionIngeniería y Arquitecturaen_US
dc.type2Artículoen_US
dc.contributor.daisngid4798827
dc.contributor.daisngid26090044
dc.contributor.daisngid32017197
dc.contributor.daisngid21103569
dc.contributor.daisngid30750692
dc.contributor.daisngid778549
dc.utils.revisionen_US
dc.contributor.wosstandardWOS:Mena, VF
dc.contributor.wosstandardWOS:Betancor-Abreu, A
dc.contributor.wosstandardWOS:Gonzalez, S
dc.contributor.wosstandardWOS:Delgado, S
dc.contributor.wosstandardWOS:Souto, RM
dc.contributor.wosstandardWOS:Santana, JJ
dc.date.coverdateSeptiembre 2019
dc.identifier.ulpgces
dc.description.sjr1,321
dc.description.jcr5,647
dc.description.sjrqQ1
dc.description.jcrqQ1
dc.description.scieSCIE
item.grantfulltextnone-
item.fulltextSin texto completo-
crisitem.author.deptGIR IUCES: Arquitectura y Concurrencia-
crisitem.author.deptIU de Cibernética, Empresa y Sociedad (IUCES)-
crisitem.author.deptDepartamento de Señales y Comunicaciones-
crisitem.author.deptGIR IDeTIC: División de Procesado Digital de Señales-
crisitem.author.deptIU para el Desarrollo Tecnológico y la Innovación-
crisitem.author.deptDepartamento de Señales y Comunicaciones-
crisitem.author.deptGIR IUSA-ONEHEALTH 3: Histología y Patología Veterinaria y Forense (Terrestre y Marina)-
crisitem.author.deptIU de Sanidad Animal y Seguridad Alimentaria-
crisitem.author.deptGIR Energía, Corrosión, Residuos y Agua-
crisitem.author.deptDepartamento de Ingeniería de Procesos-
crisitem.author.orcid0000-0003-1755-9428-
crisitem.author.orcid0000-0002-4621-2768-
crisitem.author.orcid0000-0003-1216-5446-
crisitem.author.orcid0000-0002-3030-2195-
crisitem.author.parentorgIU de Cibernética, Empresa y Sociedad (IUCES)-
crisitem.author.parentorgIU para el Desarrollo Tecnológico y la Innovación-
crisitem.author.parentorgIU de Sanidad Animal y Seguridad Alimentaria-
crisitem.author.parentorgDepartamento de Ingeniería Electrónica y Automática-
crisitem.author.fullNameMena Santana, Vicente Efigenio-
crisitem.author.fullNameTravieso González, Carlos Manuel-
crisitem.author.fullNameDiaz Delgado,Josue-
crisitem.author.fullNameSantana Rodríguez, Juan José-
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