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

Detalhes bibliográficos
Autor(a) principal: Martins, Danúbia Santiago [UNESP]
Data de Publicação: 2022
Outros Autores: Estevam, Bianca Ramos, Perez, Isadora Dias, Américo-Pinheiro, Juliana Heloisa Pinê [UNESP], Isique, William Deodato [UNESP], Boina, Rosane Freire [UNESP]
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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spelling 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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