SLUDGE FROM A WATER TREATMENT PLANT AS AN ADSORBENT OF ENDOCRINE DISRUPTORS Sludge from a water treatment plant as an adsorbent of endocrine disruptors
Autor(a) principal: | |
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Data de Publicação: | 2022 |
Outros Autores: | , , , , |
Tipo de documento: | Artigo |
Idioma: | eng |
Título da fonte: | Repositório Institucional da UNESP |
Texto Completo: | http://dx.doi.org/10.1016/j.jece.2022.108090 http://hdl.handle.net/11449/240421 |
Resumo: | Water 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. |
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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 disruptorsAbbreviations a the affinity coefficient (L.μg-1)ASAP Surface Area and Porosity Analyzerc the integration constant of the modelsC0the initial concentration (μg.L-1)Cethe equilibrium concentration (μg.L-1)Cfthe final concentration (μg.L-1)dppore diameterE2 17β EstradiolEC Emerging ContaminantsEE2 17α EthinylestradiolFTIR Fourier Transform Infrared SpectroscopyHPLC-Fl high-performance liquid chromatography coupled with a fluorescence detectorK1the velocity constant of pseudo-first-order (min-1)K2the velocity constant of pseudo-second-order (g.μg-1.min-1)KDRDubin-Radushkevich constant (mol2.kJ-2)KfFreundlich constant (μg.L-1)KlLangmuir constant (L.μg-1)KsSips constant (L.g-1)m the adsorbent mass (g)ms the heterogeneity factor (dimensionless)N Freundlich exponent (dimensionless)PAC polyaluminum chloridePAS Sludge activated with phosphoric acidPCZ point of zero chargePFO pseudo-first-orderPHS Sludge activated with potassium hydroxidePMS Physically Modified SludgePSO pseudo-second-orderqDRthe Dubinin-Radushkevich maximum adsorption capacity (μg.g-1)qeadsorption capacityqmaxthe Langmuir maximum adsorption capacity (μg.g-1)qt the adsorption capacity (μg.g-1) at time t (min)SBET surface areaSEM Scanning Electron Microscopyteequilibrium timeTGA Thermogravimetric AnalysisV the volume of solution (L)Vppore volumeWTS Water Treatment SludgeXRD X-Ray DiffractionXRF X-ray fluorescenceα the initial adsorption capacity (μg.g-1.min-1)β the extent of surface coverage and activation energy involved in the chemisorption (g.μg-1)ϵ the Polanyi potential (kJ.mol-1)Water 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.Laboratory Of Water Wastewater And Reuse-School Of Technology And Sciences São Paulo State University (UNESP), SPLaboratory Of Optimization Design And Advanced Control-School Of Chemical Engineering University Of Campinas (UNICAMP), SPDepartment Of Civil Engineering School Of Engineering São Paulo State University (UNESP), SPLaboratory Of Water Wastewater And Reuse-School Of Technology And Sciences São Paulo State University (UNESP), SPDepartment Of Civil Engineering School Of Engineering São Paulo State University (UNESP), SPUniversidade Estadual Paulista (UNESP)Universidade Estadual de Campinas (UNICAMP)Martins, Danúbia Santiago [UNESP]Estevam, Bianca RamosPerez, Isadora DiasAmérico-Pinheiro, Juliana Heloisa Pinê [UNESP]Isique, William Deodato [UNESP]Boina, Rosane Freire [UNESP]2023-03-01T20:16:27Z2023-03-01T20:16:27Z2022-08-01info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articlehttp://dx.doi.org/10.1016/j.jece.2022.108090Journal of Environmental Chemical Engineering, v. 10, n. 4, 2022.2213-3437http://hdl.handle.net/11449/24042110.1016/j.jece.2022.1080902-s2.0-85133692210Scopusreponame:Repositório Institucional da UNESPinstname:Universidade Estadual Paulista (UNESP)instacron:UNESPengJournal of Environmental Chemical Engineeringinfo:eu-repo/semantics/openAccess2023-03-01T20:16:27Zoai:repositorio.unesp.br:11449/240421Repositório InstitucionalPUBhttp://repositorio.unesp.br/oai/requestopendoar:29462024-08-05T16:37:22.916831Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)false |
dc.title.none.fl_str_mv |
SLUDGE FROM A WATER TREATMENT PLANT AS AN ADSORBENT OF ENDOCRINE DISRUPTORS Sludge from a water treatment plant as an adsorbent of endocrine disruptors |
title |
SLUDGE FROM A WATER TREATMENT PLANT AS AN ADSORBENT OF ENDOCRINE DISRUPTORS Sludge from a water treatment plant as an adsorbent of endocrine disruptors |
spellingShingle |
SLUDGE FROM A WATER TREATMENT PLANT AS AN ADSORBENT OF ENDOCRINE DISRUPTORS Sludge from a water treatment plant as an adsorbent of endocrine disruptors Martins, Danúbia Santiago [UNESP] Abbreviations a the affinity coefficient (L.μg-1) ASAP Surface Area and Porosity Analyzer c the integration constant of the models C0the initial concentration (μg.L-1) Cethe equilibrium concentration (μg.L-1) Cfthe final concentration (μg.L-1) dppore diameter E2 17β Estradiol EC Emerging Contaminants EE2 17α Ethinylestradiol FTIR Fourier Transform Infrared Spectroscopy HPLC-Fl high-performance liquid chromatography coupled with a fluorescence detector K1the velocity constant of pseudo-first-order (min-1) K2the velocity constant of pseudo-second-order (g.μg-1.min-1) KDRDubin-Radushkevich constant (mol2.kJ-2) KfFreundlich constant (μg.L-1) KlLangmuir constant (L.μg-1) KsSips constant (L.g-1) m the adsorbent mass (g) ms the heterogeneity factor (dimensionless) N Freundlich exponent (dimensionless) PAC polyaluminum chloride PAS Sludge activated with phosphoric acid PCZ point of zero charge PFO pseudo-first-order PHS Sludge activated with potassium hydroxide PMS Physically Modified Sludge PSO pseudo-second-order qDRthe Dubinin-Radushkevich maximum adsorption capacity (μg.g-1) qeadsorption capacity qmaxthe Langmuir maximum adsorption capacity (μg.g-1) qt the adsorption capacity (μg.g-1) at time t (min) SBET surface area SEM Scanning Electron Microscopy teequilibrium time TGA Thermogravimetric Analysis V the volume of solution (L) Vppore volume WTS Water Treatment Sludge XRD X-Ray Diffraction XRF X-ray fluorescence α the initial adsorption capacity (μg.g-1.min-1) β the extent of surface coverage and activation energy involved in the chemisorption (g.μg-1) ϵ the Polanyi potential (kJ.mol-1) |
title_short |
SLUDGE FROM A WATER TREATMENT PLANT AS AN ADSORBENT OF ENDOCRINE DISRUPTORS Sludge from a water treatment plant as an adsorbent of endocrine disruptors |
title_full |
SLUDGE FROM A WATER TREATMENT PLANT AS AN ADSORBENT OF ENDOCRINE DISRUPTORS Sludge from a water treatment plant as an adsorbent of endocrine disruptors |
title_fullStr |
SLUDGE FROM A WATER TREATMENT PLANT AS AN ADSORBENT OF ENDOCRINE DISRUPTORS Sludge from a water treatment plant as an adsorbent of endocrine disruptors |
title_full_unstemmed |
SLUDGE FROM A WATER TREATMENT PLANT AS AN ADSORBENT OF ENDOCRINE DISRUPTORS Sludge from a water treatment plant as an adsorbent of endocrine disruptors |
title_sort |
SLUDGE FROM A WATER TREATMENT PLANT AS AN ADSORBENT OF ENDOCRINE DISRUPTORS Sludge from a water treatment plant as an adsorbent of endocrine disruptors |
author |
Martins, Danúbia Santiago [UNESP] |
author_facet |
Martins, Danúbia Santiago [UNESP] Estevam, Bianca Ramos Perez, Isadora Dias Américo-Pinheiro, Juliana Heloisa Pinê [UNESP] Isique, William Deodato [UNESP] Boina, Rosane Freire [UNESP] |
author_role |
author |
author2 |
Estevam, Bianca Ramos Perez, Isadora Dias Américo-Pinheiro, Juliana Heloisa Pinê [UNESP] Isique, William Deodato [UNESP] Boina, Rosane Freire [UNESP] |
author2_role |
author author author author author |
dc.contributor.none.fl_str_mv |
Universidade Estadual Paulista (UNESP) Universidade Estadual de Campinas (UNICAMP) |
dc.contributor.author.fl_str_mv |
Martins, Danúbia Santiago [UNESP] Estevam, Bianca Ramos Perez, Isadora Dias Américo-Pinheiro, Juliana Heloisa Pinê [UNESP] Isique, William Deodato [UNESP] Boina, Rosane Freire [UNESP] |
dc.subject.por.fl_str_mv |
Abbreviations a the affinity coefficient (L.μg-1) ASAP Surface Area and Porosity Analyzer c the integration constant of the models C0the initial concentration (μg.L-1) Cethe equilibrium concentration (μg.L-1) Cfthe final concentration (μg.L-1) dppore diameter E2 17β Estradiol EC Emerging Contaminants EE2 17α Ethinylestradiol FTIR Fourier Transform Infrared Spectroscopy HPLC-Fl high-performance liquid chromatography coupled with a fluorescence detector K1the velocity constant of pseudo-first-order (min-1) K2the velocity constant of pseudo-second-order (g.μg-1.min-1) KDRDubin-Radushkevich constant (mol2.kJ-2) KfFreundlich constant (μg.L-1) KlLangmuir constant (L.μg-1) KsSips constant (L.g-1) m the adsorbent mass (g) ms the heterogeneity factor (dimensionless) N Freundlich exponent (dimensionless) PAC polyaluminum chloride PAS Sludge activated with phosphoric acid PCZ point of zero charge PFO pseudo-first-order PHS Sludge activated with potassium hydroxide PMS Physically Modified Sludge PSO pseudo-second-order qDRthe Dubinin-Radushkevich maximum adsorption capacity (μg.g-1) qeadsorption capacity qmaxthe Langmuir maximum adsorption capacity (μg.g-1) qt the adsorption capacity (μg.g-1) at time t (min) SBET surface area SEM Scanning Electron Microscopy teequilibrium time TGA Thermogravimetric Analysis V the volume of solution (L) Vppore volume WTS Water Treatment Sludge XRD X-Ray Diffraction XRF X-ray fluorescence α the initial adsorption capacity (μg.g-1.min-1) β the extent of surface coverage and activation energy involved in the chemisorption (g.μg-1) ϵ the Polanyi potential (kJ.mol-1) |
topic |
Abbreviations a the affinity coefficient (L.μg-1) ASAP Surface Area and Porosity Analyzer c the integration constant of the models C0the initial concentration (μg.L-1) Cethe equilibrium concentration (μg.L-1) Cfthe final concentration (μg.L-1) dppore diameter E2 17β Estradiol EC Emerging Contaminants EE2 17α Ethinylestradiol FTIR Fourier Transform Infrared Spectroscopy HPLC-Fl high-performance liquid chromatography coupled with a fluorescence detector K1the velocity constant of pseudo-first-order (min-1) K2the velocity constant of pseudo-second-order (g.μg-1.min-1) KDRDubin-Radushkevich constant (mol2.kJ-2) KfFreundlich constant (μg.L-1) KlLangmuir constant (L.μg-1) KsSips constant (L.g-1) m the adsorbent mass (g) ms the heterogeneity factor (dimensionless) N Freundlich exponent (dimensionless) PAC polyaluminum chloride PAS Sludge activated with phosphoric acid PCZ point of zero charge PFO pseudo-first-order PHS Sludge activated with potassium hydroxide PMS Physically Modified Sludge PSO pseudo-second-order qDRthe Dubinin-Radushkevich maximum adsorption capacity (μg.g-1) qeadsorption capacity qmaxthe Langmuir maximum adsorption capacity (μg.g-1) qt the adsorption capacity (μg.g-1) at time t (min) SBET surface area SEM Scanning Electron Microscopy teequilibrium time TGA Thermogravimetric Analysis V the volume of solution (L) Vppore volume WTS Water Treatment Sludge XRD X-Ray Diffraction XRF X-ray fluorescence α the initial adsorption capacity (μg.g-1.min-1) β the extent of surface coverage and activation energy involved in the chemisorption (g.μg-1) ϵ the Polanyi potential (kJ.mol-1) |
description |
Water 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. |
publishDate |
2022 |
dc.date.none.fl_str_mv |
2022-08-01 2023-03-01T20:16:27Z 2023-03-01T20:16:27Z |
dc.type.status.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/article |
format |
article |
status_str |
publishedVersion |
dc.identifier.uri.fl_str_mv |
http://dx.doi.org/10.1016/j.jece.2022.108090 Journal of Environmental Chemical Engineering, v. 10, n. 4, 2022. 2213-3437 http://hdl.handle.net/11449/240421 10.1016/j.jece.2022.108090 2-s2.0-85133692210 |
url |
http://dx.doi.org/10.1016/j.jece.2022.108090 http://hdl.handle.net/11449/240421 |
identifier_str_mv |
Journal of Environmental Chemical Engineering, v. 10, n. 4, 2022. 2213-3437 10.1016/j.jece.2022.108090 2-s2.0-85133692210 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
Journal of Environmental Chemical Engineering |
dc.rights.driver.fl_str_mv |
info:eu-repo/semantics/openAccess |
eu_rights_str_mv |
openAccess |
dc.source.none.fl_str_mv |
Scopus reponame:Repositório Institucional da UNESP instname:Universidade Estadual Paulista (UNESP) instacron:UNESP |
instname_str |
Universidade Estadual Paulista (UNESP) |
instacron_str |
UNESP |
institution |
UNESP |
reponame_str |
Repositório Institucional da UNESP |
collection |
Repositório Institucional da UNESP |
repository.name.fl_str_mv |
Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP) |
repository.mail.fl_str_mv |
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1808128679648165888 |