Reversibility of fouling on ultrafiltration membrane by backwashing and chemical cleaning: differences in organic fractions behaviour
Membrane fouling is an inherent phenomenon in ultrafiltration (UF) membrane processes, making it necessary to periodically perform backwashes (BW) and chemical cleanings in place (CIP) to restore the initial permeability of the membrane. The objective of this study was (1) to explore systematically...
| Autores: | , , , , , |
|---|---|
| Tipo de recurso: | artículo |
| Fecha de publicación: | 2016 |
| País: | España |
| Institución: | Universitat Politècnica de Catalunya (UPC) |
| Repositorio: | UPCommons. Portal del coneixement obert de la UPC |
| Idioma: | inglés |
| OAI Identifier: | oai:upcommons.upc.edu:2117/102568 |
| Acceso en línea: | https://hdl.handle.net/2117/102568 https://dx.doi.org/10.1080/19443994.2015.1022807 |
| Access Level: | acceso abierto |
| Palabra clave: | Ultrafiltration Membranes (Technology) Backwashing Fouling reversibility Organic fractions Surface water treatment Ultrafiltració Membranes (Tecnologia) Àrees temàtiques de la UPC::Enginyeria química |
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Reversibility of fouling on ultrafiltration membrane by backwashing and chemical cleaning: differences in organic fractions behaviourFerrer Mallén, OlgaLefevre, BenoitPrats, GuillemBernat Camí, XavierGibert Agulló, Oriol|||0000-0002-7313-5147Paraira Cardona, MiquelUltrafiltrationMembranes (Technology)BackwashingFouling reversibilityOrganic fractionsSurface water treatmentUltrafiltrationUltrafiltracióMembranes (Tecnologia)Àrees temàtiques de la UPC::Enginyeria químicaMembrane fouling is an inherent phenomenon in ultrafiltration (UF) membrane processes, making it necessary to periodically perform backwashes (BW) and chemical cleanings in place (CIP) to restore the initial permeability of the membrane. The objective of this study was (1) to explore systematically the effect of distinct BW-related variables (BW transmembrane pressure, duration, frequency and composition) on the reversibility of UF membrane fouling and on the permeate quality (in terms of total organic carbon, turbidity and UV absorbance) over successive filtration/BW cycles; and (2) to identify which organic fractions were most removed by the membrane and, of these, which were most detached after BW, alkaline and oxidant CIP and acid CIP episodes. For this purpose, a bench-scale outside-in hollow fibre module operated under dead-end filtration mode at constant transmembrane pressure and treating settled water from a drinking water treatment plant was employed. Dissolved organic carbon fractionation was performed by high-performance size-exclusion chromatography. Results showed that, in general, the more intensive the BW was (in terms of high transmembrane pressure, shortened frequency and prolonged duration) the more effective it was in removing fouling from the membrane. Concerning the composition of the water used for the BW, the addition of NaClO led to maximum fouling reversibility, closely followed by the combination of NaOH+NaClO, while citric acid and NaOH contributed little compared to water alone. However, results also showed that irreversible fouling was never completely avoided whatever the BW regime applied, leading to a gradual increase in the total resistance over time. Larger differences in the behaviour of the different organic fractions were observed. UF membrane preferentially retained the heaviest fraction of biopolymers (BP), while the intermediate fraction of humic substances (HS) was removed at a lower percentage and the lighter fractions seemed to entirely pass through the UF membrane. The successive application of BW and CIPs resulted in the detachment from the membrane of a significant percentage of the retained BP, whereas only a modest percentage of the retained HS.Peer Reviewed20162016-05-2020172017-03-16journal articlehttp://purl.org/coar/resource_type/c_6501AMhttp://purl.org/coar/version/c_ab4af688f83e57aainfo:eu-repo/semantics/articleapplication/pdfhttps://hdl.handle.net/2117/102568https://dx.doi.org/10.1080/19443994.2015.1022807reponame:UPCommons. Portal del coneixement obert de la UPCinstname:Universitat Politècnica de Catalunya (UPC)Inglésengopen accesshttp://purl.org/coar/access_right/c_abf2http://creativecommons.org/licenses/by-nc-nd/3.0/es/info:eu-repo/semantics/openAccessoai:upcommons.upc.edu:2117/1025682026-05-27T15:37:01Z |
| dc.title.none.fl_str_mv |
Reversibility of fouling on ultrafiltration membrane by backwashing and chemical cleaning: differences in organic fractions behaviour |
| title |
Reversibility of fouling on ultrafiltration membrane by backwashing and chemical cleaning: differences in organic fractions behaviour |
| spellingShingle |
Reversibility of fouling on ultrafiltration membrane by backwashing and chemical cleaning: differences in organic fractions behaviour Ferrer Mallén, Olga Ultrafiltration Membranes (Technology) Backwashing Fouling reversibility Organic fractions Surface water treatment Ultrafiltration Ultrafiltració Membranes (Tecnologia) Àrees temàtiques de la UPC::Enginyeria química |
| title_short |
Reversibility of fouling on ultrafiltration membrane by backwashing and chemical cleaning: differences in organic fractions behaviour |
| title_full |
Reversibility of fouling on ultrafiltration membrane by backwashing and chemical cleaning: differences in organic fractions behaviour |
| title_fullStr |
Reversibility of fouling on ultrafiltration membrane by backwashing and chemical cleaning: differences in organic fractions behaviour |
| title_full_unstemmed |
Reversibility of fouling on ultrafiltration membrane by backwashing and chemical cleaning: differences in organic fractions behaviour |
| title_sort |
Reversibility of fouling on ultrafiltration membrane by backwashing and chemical cleaning: differences in organic fractions behaviour |
| dc.creator.none.fl_str_mv |
Ferrer Mallén, Olga Lefevre, Benoit Prats, Guillem Bernat Camí, Xavier Gibert Agulló, Oriol|||0000-0002-7313-5147 Paraira Cardona, Miquel |
| author |
Ferrer Mallén, Olga |
| author_facet |
Ferrer Mallén, Olga Lefevre, Benoit Prats, Guillem Bernat Camí, Xavier Gibert Agulló, Oriol|||0000-0002-7313-5147 Paraira Cardona, Miquel |
| author_role |
author |
| author2 |
Lefevre, Benoit Prats, Guillem Bernat Camí, Xavier Gibert Agulló, Oriol|||0000-0002-7313-5147 Paraira Cardona, Miquel |
| author2_role |
author author author author author |
| dc.subject.none.fl_str_mv |
Ultrafiltration Membranes (Technology) Backwashing Fouling reversibility Organic fractions Surface water treatment Ultrafiltration Ultrafiltració Membranes (Tecnologia) Àrees temàtiques de la UPC::Enginyeria química |
| topic |
Ultrafiltration Membranes (Technology) Backwashing Fouling reversibility Organic fractions Surface water treatment Ultrafiltration Ultrafiltració Membranes (Tecnologia) Àrees temàtiques de la UPC::Enginyeria química |
| description |
Membrane fouling is an inherent phenomenon in ultrafiltration (UF) membrane processes, making it necessary to periodically perform backwashes (BW) and chemical cleanings in place (CIP) to restore the initial permeability of the membrane. The objective of this study was (1) to explore systematically the effect of distinct BW-related variables (BW transmembrane pressure, duration, frequency and composition) on the reversibility of UF membrane fouling and on the permeate quality (in terms of total organic carbon, turbidity and UV absorbance) over successive filtration/BW cycles; and (2) to identify which organic fractions were most removed by the membrane and, of these, which were most detached after BW, alkaline and oxidant CIP and acid CIP episodes. For this purpose, a bench-scale outside-in hollow fibre module operated under dead-end filtration mode at constant transmembrane pressure and treating settled water from a drinking water treatment plant was employed. Dissolved organic carbon fractionation was performed by high-performance size-exclusion chromatography. Results showed that, in general, the more intensive the BW was (in terms of high transmembrane pressure, shortened frequency and prolonged duration) the more effective it was in removing fouling from the membrane. Concerning the composition of the water used for the BW, the addition of NaClO led to maximum fouling reversibility, closely followed by the combination of NaOH+NaClO, while citric acid and NaOH contributed little compared to water alone. However, results also showed that irreversible fouling was never completely avoided whatever the BW regime applied, leading to a gradual increase in the total resistance over time. Larger differences in the behaviour of the different organic fractions were observed. UF membrane preferentially retained the heaviest fraction of biopolymers (BP), while the intermediate fraction of humic substances (HS) was removed at a lower percentage and the lighter fractions seemed to entirely pass through the UF membrane. The successive application of BW and CIPs resulted in the detachment from the membrane of a significant percentage of the retained BP, whereas only a modest percentage of the retained HS. |
| publishDate |
2016 |
| dc.date.none.fl_str_mv |
2016 2016-05-20 2017 2017-03-16 |
| dc.type.none.fl_str_mv |
journal article http://purl.org/coar/resource_type/c_6501 AM http://purl.org/coar/version/c_ab4af688f83e57aa |
| dc.type.openaire.fl_str_mv |
info:eu-repo/semantics/article |
| format |
article |
| dc.identifier.none.fl_str_mv |
https://hdl.handle.net/2117/102568 https://dx.doi.org/10.1080/19443994.2015.1022807 |
| url |
https://hdl.handle.net/2117/102568 https://dx.doi.org/10.1080/19443994.2015.1022807 |
| dc.language.none.fl_str_mv |
Inglés eng |
| language_invalid_str_mv |
Inglés |
| language |
eng |
| dc.rights.none.fl_str_mv |
open access http://purl.org/coar/access_right/c_abf2 http://creativecommons.org/licenses/by-nc-nd/3.0/es/ |
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info:eu-repo/semantics/openAccess |
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open access http://purl.org/coar/access_right/c_abf2 http://creativecommons.org/licenses/by-nc-nd/3.0/es/ |
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openAccess |
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application/pdf |
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reponame:UPCommons. Portal del coneixement obert de la UPC instname:Universitat Politècnica de Catalunya (UPC) |
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