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SLUDGE FROM A WATER TREATMENT PLANT AS AN ADSORBENT OF ENDOCRINE DISRUPTORS Sludge from a water treatment plant as an adsorbent of endocrine disruptors

dc.contributor.authorMartins, Danúbia Santiago [UNESP]
dc.contributor.authorEstevam, Bianca Ramos
dc.contributor.authorPerez, Isadora Dias
dc.contributor.authorAmérico-Pinheiro, Juliana Heloisa Pinê [UNESP]
dc.contributor.authorIsique, William Deodato [UNESP]
dc.contributor.authorBoina, Rosane Freire [UNESP]
dc.contributor.institutionUniversidade Estadual Paulista (UNESP)
dc.contributor.institutionUniversidade Estadual de Campinas (UNICAMP)
dc.date.accessioned2023-03-01T20:16:27Z
dc.date.available2023-03-01T20:16:27Z
dc.date.issued2022-08-01
dc.description.abstractWater Treatment Sludge (WTS) is a solid residue generated in large volumes. This material (in raw or modified form) was never evaluated for endocrine disruptors removal. Thus, the novelty of this work is to evaluate the removal of 17β Estradiol (E2) and 17α Ethinylestradiol (EE2) using adsorbents manufactured from WTS. The WTS underwent heat treatment, resulting in the Physically Modified Sludge (PMS). Then, PMS was chemically activated, giving rise to the sludge activated with phosphoric acid (PAS) or with potassium hydroxide (PHS). The adsorbents were characterized by TGA, ASAP, SEM, FTIR, XRD, XRF, and pH-PZC. The adsorption process was evaluated regarding the adsorbent dosage, kinetic, and isotherms. The modifications imposed on WTS were effective, increasing 1.6 times the surface area and pore volume. The adsorbents presented silica, quartz, and kaolinite in their compositions, and a pH-PZC around 6. The conditions that favor the removal of both endocrine disruptors were: 0.5 g of adsorbent, 100 μg.L-1 of initial concentration, pH of 5.5, and 240 min of stirring. PHS was the most promising adsorbent for E2 (with an adsorption capacity of 10.86 μg.g-1) and PMS for EE2 (removing 6.48 μg.g-1 of contaminant). The equilibrium time and fits kinetic models varied in function of the adsorbate concentration. The interaction between adsorbents-adsorbates occurs by chemisorption at the active sites and similar fits to Langmuir and Freundlich isotherm models were obtained. From the results obtained, a promising application for WTS residues and an alternative for E2 and EE2 removal from the aqueous solution was proposed.en
dc.description.affiliationLaboratory Of Water Wastewater And Reuse-School Of Technology And Sciences São Paulo State University (UNESP), SP
dc.description.affiliationLaboratory Of Optimization Design And Advanced Control-School Of Chemical Engineering University Of Campinas (UNICAMP), SP
dc.description.affiliationDepartment Of Civil Engineering School Of Engineering São Paulo State University (UNESP), SP
dc.description.affiliationUnespLaboratory Of Water Wastewater And Reuse-School Of Technology And Sciences São Paulo State University (UNESP), SP
dc.description.affiliationUnespDepartment Of Civil Engineering School Of Engineering São Paulo State University (UNESP), SP
dc.identifierhttp://dx.doi.org/10.1016/j.jece.2022.108090
dc.identifier.citationJournal of Environmental Chemical Engineering, v. 10, n. 4, 2022.
dc.identifier.doi10.1016/j.jece.2022.108090
dc.identifier.issn2213-3437
dc.identifier.scopus2-s2.0-85133692210
dc.identifier.urihttp://hdl.handle.net/11449/240421
dc.language.isoeng
dc.relation.ispartofJournal of Environmental Chemical Engineering
dc.sourceScopus
dc.subjectAbbreviations a the affinity coefficient (L.μg-1)
dc.subjectASAP Surface Area and Porosity Analyzer
dc.subjectc the integration constant of the models
dc.subjectC0the initial concentration (μg.L-1)
dc.subjectCethe equilibrium concentration (μg.L-1)
dc.subjectCfthe final concentration (μg.L-1)
dc.subjectdppore diameter
dc.subjectE2 17β Estradiol
dc.subjectEC Emerging Contaminants
dc.subjectEE2 17α Ethinylestradiol
dc.subjectFTIR Fourier Transform Infrared Spectroscopy
dc.subjectHPLC-Fl high-performance liquid chromatography coupled with a fluorescence detector
dc.subjectK1the velocity constant of pseudo-first-order (min-1)
dc.subjectK2the velocity constant of pseudo-second-order (g.μg-1.min-1)
dc.subjectKDRDubin-Radushkevich constant (mol2.kJ-2)
dc.subjectKfFreundlich constant (μg.L-1)
dc.subjectKlLangmuir constant (L.μg-1)
dc.subjectKsSips constant (L.g-1)
dc.subjectm the adsorbent mass (g)
dc.subjectms the heterogeneity factor (dimensionless)
dc.subjectN Freundlich exponent (dimensionless)
dc.subjectPAC polyaluminum chloride
dc.subjectPAS Sludge activated with phosphoric acid
dc.subjectPCZ point of zero charge
dc.subjectPFO pseudo-first-order
dc.subjectPHS Sludge activated with potassium hydroxide
dc.subjectPMS Physically Modified Sludge
dc.subjectPSO pseudo-second-order
dc.subjectqDRthe Dubinin-Radushkevich maximum adsorption capacity (μg.g-1)
dc.subjectqeadsorption capacity
dc.subjectqmaxthe Langmuir maximum adsorption capacity (μg.g-1)
dc.subjectqt the adsorption capacity (μg.g-1) at time t (min)
dc.subjectSBET surface area
dc.subjectSEM Scanning Electron Microscopy
dc.subjectteequilibrium time
dc.subjectTGA Thermogravimetric Analysis
dc.subjectV the volume of solution (L)
dc.subjectVppore volume
dc.subjectWTS Water Treatment Sludge
dc.subjectXRD X-Ray Diffraction
dc.subjectXRF X-ray fluorescence
dc.subjectα the initial adsorption capacity (μg.g-1.min-1)
dc.subjectβ the extent of surface coverage and activation energy involved in the chemisorption (g.μg-1)
dc.subjectϵ the Polanyi potential (kJ.mol-1)
dc.titleSLUDGE FROM A WATER TREATMENT PLANT AS AN ADSORBENT OF ENDOCRINE DISRUPTORS Sludge from a water treatment plant as an adsorbent of endocrine disruptorsen
dc.typeArtigopt
dspace.entity.typePublication
relation.isOrgUnitOfPublicationbbcf06b3-c5f9-4a27-ac03-b690202a3b4e
relation.isOrgUnitOfPublication.latestForDiscoverybbcf06b3-c5f9-4a27-ac03-b690202a3b4e
unesp.campusUniversidade Estadual Paulista (UNESP), Faculdade de Ciências e Tecnologia, Presidente Prudentept

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