Water Defluoridation: Nanofiltration vs Membrane Distillation

Autores
Morán Ayala, Lucía Isabel; Paquet, Marie; Janowska, Katarzyna Joanna; Jamard, Paul; Quist-Jensen, Cejna Anna; Bosio, Gabriela Natalia; Mártire, Daniel Osvaldo; Fabbri, Debora; Boffa, Vittorio
Año de publicación
2018
Idioma
inglés
Tipo de recurso
artículo
Estado
versión publicada
Descripción
Nowadays, fluoride contamination of drinking water is a major problem for various countries, because high concentrations of fluoride pose a risk of dental and skeletal fluorosis. Over past years, membrane nanofiltration (NF) has been proposed as convenient defluoridation technology. However, NF cannot be applied to water systems with high fluoride concentration, and the disposal of the membrane concentrate remains an issue. In this work, we compared a commercial polyester NF membrane and a polypropylene hollowfiber membrane distillation (MD) module for their ability to remove fluoride ions from water in the presence of hardness ions and organic fouling agents. The NF membrane can offer more than 10 times higher water productivity than MD, under realistic gradients of temperature and pressure, respectively. Despite that, after reaching a concentration factor of about 3, fouling and scaling caused the flux to drop to about 80% with respect to its initial value. Moreover, F− retention decreased from 90% to below 80%, thus providing a permeate of scarce quality. MD was operated in the direct-contact mode on a polypropylene hollowfiber membrane, which was charged with a hot feed flow (average T = 58 °C) on one side and a cooled (20 °C) permeate flow of distilled water on the other side. The concentration of fluoride ions in the permeate was always below the detection limit of our electrode (0.2 ppm), regardless of the fluoride concentration in the feed. Moreover, the MD module showed higher resistance to fouling and scaling than NF, and CaF2 crystals were recovered from the MD concentrate after cooling. These results suggest that the synergic combination of the two techniques might be beneficial for the purification of fluoridecontaminated water systems: MD can be used to further concentrate the NF retentate, thus producing high-purity water and recovering CaF2 crystals.
Instituto de Investigaciones Fisicoquímicas Teóricas y Aplicadas
Materia
Química
Anions
Ions
Membranes
Animal feed
Filtration
Nivel de accesibilidad
acceso abierto
Condiciones de uso
http://creativecommons.org/licenses/by-nc/4.0/
Repositorio
SEDICI (UNLP)
Institución
Universidad Nacional de La Plata
OAI Identificador
oai:sedici.unlp.edu.ar:10915/123548

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oai_identifier_str oai:sedici.unlp.edu.ar:10915/123548
network_acronym_str SEDICI
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network_name_str SEDICI (UNLP)
spelling Water Defluoridation: Nanofiltration vs Membrane DistillationMorán Ayala, Lucía IsabelPaquet, MarieJanowska, Katarzyna JoannaJamard, PaulQuist-Jensen, Cejna AnnaBosio, Gabriela NataliaMártire, Daniel OsvaldoFabbri, DeboraBoffa, VittorioQuímicaAnionsIonsMembranesAnimal feedFiltrationNowadays, fluoride contamination of drinking water is a major problem for various countries, because high concentrations of fluoride pose a risk of dental and skeletal fluorosis. Over past years, membrane nanofiltration (NF) has been proposed as convenient defluoridation technology. However, NF cannot be applied to water systems with high fluoride concentration, and the disposal of the membrane concentrate remains an issue. In this work, we compared a commercial polyester NF membrane and a polypropylene hollowfiber membrane distillation (MD) module for their ability to remove fluoride ions from water in the presence of hardness ions and organic fouling agents. The NF membrane can offer more than 10 times higher water productivity than MD, under realistic gradients of temperature and pressure, respectively. Despite that, after reaching a concentration factor of about 3, fouling and scaling caused the flux to drop to about 80% with respect to its initial value. Moreover, F− retention decreased from 90% to below 80%, thus providing a permeate of scarce quality. MD was operated in the direct-contact mode on a polypropylene hollowfiber membrane, which was charged with a hot feed flow (average T = 58 °C) on one side and a cooled (20 °C) permeate flow of distilled water on the other side. The concentration of fluoride ions in the permeate was always below the detection limit of our electrode (0.2 ppm), regardless of the fluoride concentration in the feed. Moreover, the MD module showed higher resistance to fouling and scaling than NF, and CaF2 crystals were recovered from the MD concentrate after cooling. These results suggest that the synergic combination of the two techniques might be beneficial for the purification of fluoridecontaminated water systems: MD can be used to further concentrate the NF retentate, thus producing high-purity water and recovering CaF2 crystals.Instituto de Investigaciones Fisicoquímicas Teóricas y Aplicadas2018info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionArticulohttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdf14740-14748http://sedici.unlp.edu.ar/handle/10915/123548enginfo:eu-repo/semantics/altIdentifier/issn/0888-5885info:eu-repo/semantics/altIdentifier/issn/1520-5045info:eu-repo/semantics/altIdentifier/doi/10.1021/acs.iecr.8b03620info:eu-repo/semantics/openAccesshttp://creativecommons.org/licenses/by-nc/4.0/Creative Commons Attribution-NonCommercial 4.0 International (CC BY-NC 4.0)reponame:SEDICI (UNLP)instname:Universidad Nacional de La Platainstacron:UNLP2025-10-15T11:21:22Zoai:sedici.unlp.edu.ar:10915/123548Institucionalhttp://sedici.unlp.edu.ar/Universidad públicaNo correspondehttp://sedici.unlp.edu.ar/oai/snrdalira@sedici.unlp.edu.arArgentinaNo correspondeNo correspondeNo correspondeopendoar:13292025-10-15 11:21:22.385SEDICI (UNLP) - Universidad Nacional de La Platafalse
dc.title.none.fl_str_mv Water Defluoridation: Nanofiltration vs Membrane Distillation
title Water Defluoridation: Nanofiltration vs Membrane Distillation
spellingShingle Water Defluoridation: Nanofiltration vs Membrane Distillation
Morán Ayala, Lucía Isabel
Química
Anions
Ions
Membranes
Animal feed
Filtration
title_short Water Defluoridation: Nanofiltration vs Membrane Distillation
title_full Water Defluoridation: Nanofiltration vs Membrane Distillation
title_fullStr Water Defluoridation: Nanofiltration vs Membrane Distillation
title_full_unstemmed Water Defluoridation: Nanofiltration vs Membrane Distillation
title_sort Water Defluoridation: Nanofiltration vs Membrane Distillation
dc.creator.none.fl_str_mv Morán Ayala, Lucía Isabel
Paquet, Marie
Janowska, Katarzyna Joanna
Jamard, Paul
Quist-Jensen, Cejna Anna
Bosio, Gabriela Natalia
Mártire, Daniel Osvaldo
Fabbri, Debora
Boffa, Vittorio
author Morán Ayala, Lucía Isabel
author_facet Morán Ayala, Lucía Isabel
Paquet, Marie
Janowska, Katarzyna Joanna
Jamard, Paul
Quist-Jensen, Cejna Anna
Bosio, Gabriela Natalia
Mártire, Daniel Osvaldo
Fabbri, Debora
Boffa, Vittorio
author_role author
author2 Paquet, Marie
Janowska, Katarzyna Joanna
Jamard, Paul
Quist-Jensen, Cejna Anna
Bosio, Gabriela Natalia
Mártire, Daniel Osvaldo
Fabbri, Debora
Boffa, Vittorio
author2_role author
author
author
author
author
author
author
author
dc.subject.none.fl_str_mv Química
Anions
Ions
Membranes
Animal feed
Filtration
topic Química
Anions
Ions
Membranes
Animal feed
Filtration
dc.description.none.fl_txt_mv Nowadays, fluoride contamination of drinking water is a major problem for various countries, because high concentrations of fluoride pose a risk of dental and skeletal fluorosis. Over past years, membrane nanofiltration (NF) has been proposed as convenient defluoridation technology. However, NF cannot be applied to water systems with high fluoride concentration, and the disposal of the membrane concentrate remains an issue. In this work, we compared a commercial polyester NF membrane and a polypropylene hollowfiber membrane distillation (MD) module for their ability to remove fluoride ions from water in the presence of hardness ions and organic fouling agents. The NF membrane can offer more than 10 times higher water productivity than MD, under realistic gradients of temperature and pressure, respectively. Despite that, after reaching a concentration factor of about 3, fouling and scaling caused the flux to drop to about 80% with respect to its initial value. Moreover, F− retention decreased from 90% to below 80%, thus providing a permeate of scarce quality. MD was operated in the direct-contact mode on a polypropylene hollowfiber membrane, which was charged with a hot feed flow (average T = 58 °C) on one side and a cooled (20 °C) permeate flow of distilled water on the other side. The concentration of fluoride ions in the permeate was always below the detection limit of our electrode (0.2 ppm), regardless of the fluoride concentration in the feed. Moreover, the MD module showed higher resistance to fouling and scaling than NF, and CaF2 crystals were recovered from the MD concentrate after cooling. These results suggest that the synergic combination of the two techniques might be beneficial for the purification of fluoridecontaminated water systems: MD can be used to further concentrate the NF retentate, thus producing high-purity water and recovering CaF2 crystals.
Instituto de Investigaciones Fisicoquímicas Teóricas y Aplicadas
description Nowadays, fluoride contamination of drinking water is a major problem for various countries, because high concentrations of fluoride pose a risk of dental and skeletal fluorosis. Over past years, membrane nanofiltration (NF) has been proposed as convenient defluoridation technology. However, NF cannot be applied to water systems with high fluoride concentration, and the disposal of the membrane concentrate remains an issue. In this work, we compared a commercial polyester NF membrane and a polypropylene hollowfiber membrane distillation (MD) module for their ability to remove fluoride ions from water in the presence of hardness ions and organic fouling agents. The NF membrane can offer more than 10 times higher water productivity than MD, under realistic gradients of temperature and pressure, respectively. Despite that, after reaching a concentration factor of about 3, fouling and scaling caused the flux to drop to about 80% with respect to its initial value. Moreover, F− retention decreased from 90% to below 80%, thus providing a permeate of scarce quality. MD was operated in the direct-contact mode on a polypropylene hollowfiber membrane, which was charged with a hot feed flow (average T = 58 °C) on one side and a cooled (20 °C) permeate flow of distilled water on the other side. The concentration of fluoride ions in the permeate was always below the detection limit of our electrode (0.2 ppm), regardless of the fluoride concentration in the feed. Moreover, the MD module showed higher resistance to fouling and scaling than NF, and CaF2 crystals were recovered from the MD concentrate after cooling. These results suggest that the synergic combination of the two techniques might be beneficial for the purification of fluoridecontaminated water systems: MD can be used to further concentrate the NF retentate, thus producing high-purity water and recovering CaF2 crystals.
publishDate 2018
dc.date.none.fl_str_mv 2018
dc.type.none.fl_str_mv info:eu-repo/semantics/article
info:eu-repo/semantics/publishedVersion
Articulo
http://purl.org/coar/resource_type/c_6501
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format article
status_str publishedVersion
dc.identifier.none.fl_str_mv http://sedici.unlp.edu.ar/handle/10915/123548
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dc.language.none.fl_str_mv eng
language eng
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info:eu-repo/semantics/altIdentifier/issn/1520-5045
info:eu-repo/semantics/altIdentifier/doi/10.1021/acs.iecr.8b03620
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http://creativecommons.org/licenses/by-nc/4.0/
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