Removal of aqueous nC60 fullerene from water by low pressure membrane filtration
The potential environmental and health risks of engineered nanoparticles such as buckminsterfullerene C60 in water require their removal during the production of drinking water. We present a study focusing on (i) the removal mechanism and (ii) the elucidation of the role of the membrane pore size du...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Floris, R [verfasserIn] |
|---|
| Format: |
Artikel |
|---|---|
| Sprache: |
Englisch |
| Erschienen: |
2016 |
|---|
| Rechteinformationen: |
Nutzungsrecht: Copyright © 2015 Elsevier Ltd. All rights reserved. |
|---|
| Übergeordnetes Werk: |
Enthalten in: Water research - Amsterdam [u.a.] : Elsevier, Pergamon, 1967, 91(2016), Seite 115-125 |
|---|---|
| Übergeordnetes Werk: |
volume:91 ; year:2016 ; pages:115-125 |
| Links: |
|---|
| DOI / URN: |
10.1016/j.watres.2015.10.014 |
|---|
| Katalog-ID: |
OLC1972595830 |
|---|
| LEADER | 01000caa a2200265 4500 | ||
|---|---|---|---|
| 001 | OLC1972595830 | ||
| 003 | DE-627 | ||
| 005 | 20230714183308.0 | ||
| 007 | tu | ||
| 008 | 160427s2016 xx ||||| 00| ||eng c | ||
| 024 | 7 | |a 10.1016/j.watres.2015.10.014 |2 doi | |
| 028 | 5 | 2 | |a PQ20160430 |
| 035 | |a (DE-627)OLC1972595830 | ||
| 035 | |a (DE-599)GBVOLC1972595830 | ||
| 035 | |a (PRQ)c1214-a350cdae474877f5b69cbf615829540b980f5465f227db77ffd161d59f3e36590 | ||
| 035 | |a (KEY)0018203620160000091000000115removalofaqueousnc60fullerenefromwaterbylowpressur | ||
| 040 | |a DE-627 |b ger |c DE-627 |e rakwb | ||
| 041 | |a eng | ||
| 082 | 0 | 4 | |a 550 |q DNB |
| 100 | 1 | |a Floris, R |e verfasserin |4 aut | |
| 245 | 1 | 0 | |a Removal of aqueous nC60 fullerene from water by low pressure membrane filtration |
| 264 | 1 | |c 2016 | |
| 336 | |a Text |b txt |2 rdacontent | ||
| 337 | |a ohne Hilfsmittel zu benutzen |b n |2 rdamedia | ||
| 338 | |a Band |b nc |2 rdacarrier | ||
| 520 | |a The potential environmental and health risks of engineered nanoparticles such as buckminsterfullerene C60 in water require their removal during the production of drinking water. We present a study focusing on (i) the removal mechanism and (ii) the elucidation of the role of the membrane pore size during removal of nC60 fullerene nanoparticle suspensions in dead-end microfiltration and ultrafiltration mimicking separation in real industrial water treatment plants. Membranes were selected with pore sizes ranging from 18 nm to 500 nm to determine the significance of the nC60 to membrane pore size ratio and the adsorption affinity between nC60 and membrane material during filtration. Experiments were carried out with a dead-end bench-scale system operated at constant flux conditions including a hydraulic backwash cleaning procedure. nC60 nanoparticles can be efficiently removed by low pressure membrane technology with smaller and, unexpectedly, also by mostly similar or larger pores than the particle size, although the nC60 filtration behaviour appeared to be different. The nC60 size to membrane pore size ratio and the ratio of the cake-layer deposition resistance to the clean membrane resistance, both play an important role on the nC60 filtration behaviour and on the efficiency of the backwash procedure recovering the initial membrane filtration conditions. These results become specifically significant in the context of drinking water production, for which they provide relevant information for an accurate selection between membrane processes and operational parameters for the removal of nC60 in the drinking water treatment. | ||
| 540 | |a Nutzungsrecht: Copyright © 2015 Elsevier Ltd. All rights reserved. | ||
| 700 | 1 | |a Nijmeijer, K |4 oth | |
| 700 | 1 | |a Cornelissen, E R |4 oth | |
| 773 | 0 | 8 | |i Enthalten in |t Water research |d Amsterdam [u.a.] : Elsevier, Pergamon, 1967 |g 91(2016), Seite 115-125 |w (DE-627)129471860 |w (DE-600)202613-2 |w (DE-576)014841630 |x 0043-1354 |7 nnns |
| 773 | 1 | 8 | |g volume:91 |g year:2016 |g pages:115-125 |
| 856 | 4 | 1 | |u http://dx.doi.org/10.1016/j.watres.2015.10.014 |3 Volltext |
| 856 | 4 | 2 | |u http://www.ncbi.nlm.nih.gov/pubmed/26773485 |
| 912 | |a GBV_USEFLAG_A | ||
| 912 | |a SYSFLAG_A | ||
| 912 | |a GBV_OLC | ||
| 912 | |a SSG-OLC-UMW | ||
| 912 | |a SSG-OLC-TEC | ||
| 912 | |a SSG-OPC-GGO | ||
| 912 | |a GBV_ILN_20 | ||
| 912 | |a GBV_ILN_21 | ||
| 912 | |a GBV_ILN_70 | ||
| 912 | |a GBV_ILN_4112 | ||
| 912 | |a GBV_ILN_4219 | ||
| 951 | |a AR | ||
| 952 | |d 91 |j 2016 |h 115-125 | ||
| author_variant |
r f rf |
|---|---|
| matchkey_str |
article:00431354:2016----::eoaoauosc0ulrnfowtryopesr |
| hierarchy_sort_str |
2016 |
| publishDate |
2016 |
| allfields |
10.1016/j.watres.2015.10.014 doi PQ20160430 (DE-627)OLC1972595830 (DE-599)GBVOLC1972595830 (PRQ)c1214-a350cdae474877f5b69cbf615829540b980f5465f227db77ffd161d59f3e36590 (KEY)0018203620160000091000000115removalofaqueousnc60fullerenefromwaterbylowpressur DE-627 ger DE-627 rakwb eng 550 DNB Floris, R verfasserin aut Removal of aqueous nC60 fullerene from water by low pressure membrane filtration 2016 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier The potential environmental and health risks of engineered nanoparticles such as buckminsterfullerene C60 in water require their removal during the production of drinking water. We present a study focusing on (i) the removal mechanism and (ii) the elucidation of the role of the membrane pore size during removal of nC60 fullerene nanoparticle suspensions in dead-end microfiltration and ultrafiltration mimicking separation in real industrial water treatment plants. Membranes were selected with pore sizes ranging from 18 nm to 500 nm to determine the significance of the nC60 to membrane pore size ratio and the adsorption affinity between nC60 and membrane material during filtration. Experiments were carried out with a dead-end bench-scale system operated at constant flux conditions including a hydraulic backwash cleaning procedure. nC60 nanoparticles can be efficiently removed by low pressure membrane technology with smaller and, unexpectedly, also by mostly similar or larger pores than the particle size, although the nC60 filtration behaviour appeared to be different. The nC60 size to membrane pore size ratio and the ratio of the cake-layer deposition resistance to the clean membrane resistance, both play an important role on the nC60 filtration behaviour and on the efficiency of the backwash procedure recovering the initial membrane filtration conditions. These results become specifically significant in the context of drinking water production, for which they provide relevant information for an accurate selection between membrane processes and operational parameters for the removal of nC60 in the drinking water treatment. Nutzungsrecht: Copyright © 2015 Elsevier Ltd. All rights reserved. Nijmeijer, K oth Cornelissen, E R oth Enthalten in Water research Amsterdam [u.a.] : Elsevier, Pergamon, 1967 91(2016), Seite 115-125 (DE-627)129471860 (DE-600)202613-2 (DE-576)014841630 0043-1354 nnns volume:91 year:2016 pages:115-125 http://dx.doi.org/10.1016/j.watres.2015.10.014 Volltext http://www.ncbi.nlm.nih.gov/pubmed/26773485 GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-TEC SSG-OPC-GGO GBV_ILN_20 GBV_ILN_21 GBV_ILN_70 GBV_ILN_4112 GBV_ILN_4219 AR 91 2016 115-125 |
| spelling |
10.1016/j.watres.2015.10.014 doi PQ20160430 (DE-627)OLC1972595830 (DE-599)GBVOLC1972595830 (PRQ)c1214-a350cdae474877f5b69cbf615829540b980f5465f227db77ffd161d59f3e36590 (KEY)0018203620160000091000000115removalofaqueousnc60fullerenefromwaterbylowpressur DE-627 ger DE-627 rakwb eng 550 DNB Floris, R verfasserin aut Removal of aqueous nC60 fullerene from water by low pressure membrane filtration 2016 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier The potential environmental and health risks of engineered nanoparticles such as buckminsterfullerene C60 in water require their removal during the production of drinking water. We present a study focusing on (i) the removal mechanism and (ii) the elucidation of the role of the membrane pore size during removal of nC60 fullerene nanoparticle suspensions in dead-end microfiltration and ultrafiltration mimicking separation in real industrial water treatment plants. Membranes were selected with pore sizes ranging from 18 nm to 500 nm to determine the significance of the nC60 to membrane pore size ratio and the adsorption affinity between nC60 and membrane material during filtration. Experiments were carried out with a dead-end bench-scale system operated at constant flux conditions including a hydraulic backwash cleaning procedure. nC60 nanoparticles can be efficiently removed by low pressure membrane technology with smaller and, unexpectedly, also by mostly similar or larger pores than the particle size, although the nC60 filtration behaviour appeared to be different. The nC60 size to membrane pore size ratio and the ratio of the cake-layer deposition resistance to the clean membrane resistance, both play an important role on the nC60 filtration behaviour and on the efficiency of the backwash procedure recovering the initial membrane filtration conditions. These results become specifically significant in the context of drinking water production, for which they provide relevant information for an accurate selection between membrane processes and operational parameters for the removal of nC60 in the drinking water treatment. Nutzungsrecht: Copyright © 2015 Elsevier Ltd. All rights reserved. Nijmeijer, K oth Cornelissen, E R oth Enthalten in Water research Amsterdam [u.a.] : Elsevier, Pergamon, 1967 91(2016), Seite 115-125 (DE-627)129471860 (DE-600)202613-2 (DE-576)014841630 0043-1354 nnns volume:91 year:2016 pages:115-125 http://dx.doi.org/10.1016/j.watres.2015.10.014 Volltext http://www.ncbi.nlm.nih.gov/pubmed/26773485 GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-TEC SSG-OPC-GGO GBV_ILN_20 GBV_ILN_21 GBV_ILN_70 GBV_ILN_4112 GBV_ILN_4219 AR 91 2016 115-125 |
| allfields_unstemmed |
10.1016/j.watres.2015.10.014 doi PQ20160430 (DE-627)OLC1972595830 (DE-599)GBVOLC1972595830 (PRQ)c1214-a350cdae474877f5b69cbf615829540b980f5465f227db77ffd161d59f3e36590 (KEY)0018203620160000091000000115removalofaqueousnc60fullerenefromwaterbylowpressur DE-627 ger DE-627 rakwb eng 550 DNB Floris, R verfasserin aut Removal of aqueous nC60 fullerene from water by low pressure membrane filtration 2016 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier The potential environmental and health risks of engineered nanoparticles such as buckminsterfullerene C60 in water require their removal during the production of drinking water. We present a study focusing on (i) the removal mechanism and (ii) the elucidation of the role of the membrane pore size during removal of nC60 fullerene nanoparticle suspensions in dead-end microfiltration and ultrafiltration mimicking separation in real industrial water treatment plants. Membranes were selected with pore sizes ranging from 18 nm to 500 nm to determine the significance of the nC60 to membrane pore size ratio and the adsorption affinity between nC60 and membrane material during filtration. Experiments were carried out with a dead-end bench-scale system operated at constant flux conditions including a hydraulic backwash cleaning procedure. nC60 nanoparticles can be efficiently removed by low pressure membrane technology with smaller and, unexpectedly, also by mostly similar or larger pores than the particle size, although the nC60 filtration behaviour appeared to be different. The nC60 size to membrane pore size ratio and the ratio of the cake-layer deposition resistance to the clean membrane resistance, both play an important role on the nC60 filtration behaviour and on the efficiency of the backwash procedure recovering the initial membrane filtration conditions. These results become specifically significant in the context of drinking water production, for which they provide relevant information for an accurate selection between membrane processes and operational parameters for the removal of nC60 in the drinking water treatment. Nutzungsrecht: Copyright © 2015 Elsevier Ltd. All rights reserved. Nijmeijer, K oth Cornelissen, E R oth Enthalten in Water research Amsterdam [u.a.] : Elsevier, Pergamon, 1967 91(2016), Seite 115-125 (DE-627)129471860 (DE-600)202613-2 (DE-576)014841630 0043-1354 nnns volume:91 year:2016 pages:115-125 http://dx.doi.org/10.1016/j.watres.2015.10.014 Volltext http://www.ncbi.nlm.nih.gov/pubmed/26773485 GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-TEC SSG-OPC-GGO GBV_ILN_20 GBV_ILN_21 GBV_ILN_70 GBV_ILN_4112 GBV_ILN_4219 AR 91 2016 115-125 |
| allfieldsGer |
10.1016/j.watres.2015.10.014 doi PQ20160430 (DE-627)OLC1972595830 (DE-599)GBVOLC1972595830 (PRQ)c1214-a350cdae474877f5b69cbf615829540b980f5465f227db77ffd161d59f3e36590 (KEY)0018203620160000091000000115removalofaqueousnc60fullerenefromwaterbylowpressur DE-627 ger DE-627 rakwb eng 550 DNB Floris, R verfasserin aut Removal of aqueous nC60 fullerene from water by low pressure membrane filtration 2016 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier The potential environmental and health risks of engineered nanoparticles such as buckminsterfullerene C60 in water require their removal during the production of drinking water. We present a study focusing on (i) the removal mechanism and (ii) the elucidation of the role of the membrane pore size during removal of nC60 fullerene nanoparticle suspensions in dead-end microfiltration and ultrafiltration mimicking separation in real industrial water treatment plants. Membranes were selected with pore sizes ranging from 18 nm to 500 nm to determine the significance of the nC60 to membrane pore size ratio and the adsorption affinity between nC60 and membrane material during filtration. Experiments were carried out with a dead-end bench-scale system operated at constant flux conditions including a hydraulic backwash cleaning procedure. nC60 nanoparticles can be efficiently removed by low pressure membrane technology with smaller and, unexpectedly, also by mostly similar or larger pores than the particle size, although the nC60 filtration behaviour appeared to be different. The nC60 size to membrane pore size ratio and the ratio of the cake-layer deposition resistance to the clean membrane resistance, both play an important role on the nC60 filtration behaviour and on the efficiency of the backwash procedure recovering the initial membrane filtration conditions. These results become specifically significant in the context of drinking water production, for which they provide relevant information for an accurate selection between membrane processes and operational parameters for the removal of nC60 in the drinking water treatment. Nutzungsrecht: Copyright © 2015 Elsevier Ltd. All rights reserved. Nijmeijer, K oth Cornelissen, E R oth Enthalten in Water research Amsterdam [u.a.] : Elsevier, Pergamon, 1967 91(2016), Seite 115-125 (DE-627)129471860 (DE-600)202613-2 (DE-576)014841630 0043-1354 nnns volume:91 year:2016 pages:115-125 http://dx.doi.org/10.1016/j.watres.2015.10.014 Volltext http://www.ncbi.nlm.nih.gov/pubmed/26773485 GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-TEC SSG-OPC-GGO GBV_ILN_20 GBV_ILN_21 GBV_ILN_70 GBV_ILN_4112 GBV_ILN_4219 AR 91 2016 115-125 |
| allfieldsSound |
10.1016/j.watres.2015.10.014 doi PQ20160430 (DE-627)OLC1972595830 (DE-599)GBVOLC1972595830 (PRQ)c1214-a350cdae474877f5b69cbf615829540b980f5465f227db77ffd161d59f3e36590 (KEY)0018203620160000091000000115removalofaqueousnc60fullerenefromwaterbylowpressur DE-627 ger DE-627 rakwb eng 550 DNB Floris, R verfasserin aut Removal of aqueous nC60 fullerene from water by low pressure membrane filtration 2016 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier The potential environmental and health risks of engineered nanoparticles such as buckminsterfullerene C60 in water require their removal during the production of drinking water. We present a study focusing on (i) the removal mechanism and (ii) the elucidation of the role of the membrane pore size during removal of nC60 fullerene nanoparticle suspensions in dead-end microfiltration and ultrafiltration mimicking separation in real industrial water treatment plants. Membranes were selected with pore sizes ranging from 18 nm to 500 nm to determine the significance of the nC60 to membrane pore size ratio and the adsorption affinity between nC60 and membrane material during filtration. Experiments were carried out with a dead-end bench-scale system operated at constant flux conditions including a hydraulic backwash cleaning procedure. nC60 nanoparticles can be efficiently removed by low pressure membrane technology with smaller and, unexpectedly, also by mostly similar or larger pores than the particle size, although the nC60 filtration behaviour appeared to be different. The nC60 size to membrane pore size ratio and the ratio of the cake-layer deposition resistance to the clean membrane resistance, both play an important role on the nC60 filtration behaviour and on the efficiency of the backwash procedure recovering the initial membrane filtration conditions. These results become specifically significant in the context of drinking water production, for which they provide relevant information for an accurate selection between membrane processes and operational parameters for the removal of nC60 in the drinking water treatment. Nutzungsrecht: Copyright © 2015 Elsevier Ltd. All rights reserved. Nijmeijer, K oth Cornelissen, E R oth Enthalten in Water research Amsterdam [u.a.] : Elsevier, Pergamon, 1967 91(2016), Seite 115-125 (DE-627)129471860 (DE-600)202613-2 (DE-576)014841630 0043-1354 nnns volume:91 year:2016 pages:115-125 http://dx.doi.org/10.1016/j.watres.2015.10.014 Volltext http://www.ncbi.nlm.nih.gov/pubmed/26773485 GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-TEC SSG-OPC-GGO GBV_ILN_20 GBV_ILN_21 GBV_ILN_70 GBV_ILN_4112 GBV_ILN_4219 AR 91 2016 115-125 |
| language |
English |
| source |
Enthalten in Water research 91(2016), Seite 115-125 volume:91 year:2016 pages:115-125 |
| sourceStr |
Enthalten in Water research 91(2016), Seite 115-125 volume:91 year:2016 pages:115-125 |
| format_phy_str_mv |
Article |
| institution |
findex.gbv.de |
| dewey-raw |
550 |
| isfreeaccess_bool |
false |
| container_title |
Water research |
| authorswithroles_txt_mv |
Floris, R @@aut@@ Nijmeijer, K @@oth@@ Cornelissen, E R @@oth@@ |
| publishDateDaySort_date |
2016-01-01T00:00:00Z |
| hierarchy_top_id |
129471860 |
| dewey-sort |
3550 |
| id |
OLC1972595830 |
| language_de |
englisch |
| fullrecord |
<?xml version="1.0" encoding="UTF-8"?><collection xmlns="http://www.loc.gov/MARC21/slim"><record><leader>01000caa a2200265 4500</leader><controlfield tag="001">OLC1972595830</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20230714183308.0</controlfield><controlfield tag="007">tu</controlfield><controlfield tag="008">160427s2016 xx ||||| 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.1016/j.watres.2015.10.014</subfield><subfield code="2">doi</subfield></datafield><datafield tag="028" ind1="5" ind2="2"><subfield code="a">PQ20160430</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)OLC1972595830</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-599)GBVOLC1972595830</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(PRQ)c1214-a350cdae474877f5b69cbf615829540b980f5465f227db77ffd161d59f3e36590</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(KEY)0018203620160000091000000115removalofaqueousnc60fullerenefromwaterbylowpressur</subfield></datafield><datafield tag="040" ind1=" " ind2=" "><subfield code="a">DE-627</subfield><subfield code="b">ger</subfield><subfield code="c">DE-627</subfield><subfield code="e">rakwb</subfield></datafield><datafield tag="041" ind1=" " ind2=" "><subfield code="a">eng</subfield></datafield><datafield tag="082" ind1="0" ind2="4"><subfield code="a">550</subfield><subfield code="q">DNB</subfield></datafield><datafield tag="100" ind1="1" ind2=" "><subfield code="a">Floris, R</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Removal of aqueous nC60 fullerene from water by low pressure membrane filtration</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2016</subfield></datafield><datafield tag="336" ind1=" " ind2=" "><subfield code="a">Text</subfield><subfield code="b">txt</subfield><subfield code="2">rdacontent</subfield></datafield><datafield tag="337" ind1=" " ind2=" "><subfield code="a">ohne Hilfsmittel zu benutzen</subfield><subfield code="b">n</subfield><subfield code="2">rdamedia</subfield></datafield><datafield tag="338" ind1=" " ind2=" "><subfield code="a">Band</subfield><subfield code="b">nc</subfield><subfield code="2">rdacarrier</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">The potential environmental and health risks of engineered nanoparticles such as buckminsterfullerene C60 in water require their removal during the production of drinking water. We present a study focusing on (i) the removal mechanism and (ii) the elucidation of the role of the membrane pore size during removal of nC60 fullerene nanoparticle suspensions in dead-end microfiltration and ultrafiltration mimicking separation in real industrial water treatment plants. Membranes were selected with pore sizes ranging from 18 nm to 500 nm to determine the significance of the nC60 to membrane pore size ratio and the adsorption affinity between nC60 and membrane material during filtration. Experiments were carried out with a dead-end bench-scale system operated at constant flux conditions including a hydraulic backwash cleaning procedure. nC60 nanoparticles can be efficiently removed by low pressure membrane technology with smaller and, unexpectedly, also by mostly similar or larger pores than the particle size, although the nC60 filtration behaviour appeared to be different. The nC60 size to membrane pore size ratio and the ratio of the cake-layer deposition resistance to the clean membrane resistance, both play an important role on the nC60 filtration behaviour and on the efficiency of the backwash procedure recovering the initial membrane filtration conditions. These results become specifically significant in the context of drinking water production, for which they provide relevant information for an accurate selection between membrane processes and operational parameters for the removal of nC60 in the drinking water treatment.</subfield></datafield><datafield tag="540" ind1=" " ind2=" "><subfield code="a">Nutzungsrecht: Copyright © 2015 Elsevier Ltd. All rights reserved.</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Nijmeijer, K</subfield><subfield code="4">oth</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Cornelissen, E R</subfield><subfield code="4">oth</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">Enthalten in</subfield><subfield code="t">Water research</subfield><subfield code="d">Amsterdam [u.a.] : Elsevier, Pergamon, 1967</subfield><subfield code="g">91(2016), Seite 115-125</subfield><subfield code="w">(DE-627)129471860</subfield><subfield code="w">(DE-600)202613-2</subfield><subfield code="w">(DE-576)014841630</subfield><subfield code="x">0043-1354</subfield><subfield code="7">nnns</subfield></datafield><datafield tag="773" ind1="1" ind2="8"><subfield code="g">volume:91</subfield><subfield code="g">year:2016</subfield><subfield code="g">pages:115-125</subfield></datafield><datafield tag="856" ind1="4" ind2="1"><subfield code="u">http://dx.doi.org/10.1016/j.watres.2015.10.014</subfield><subfield code="3">Volltext</subfield></datafield><datafield tag="856" ind1="4" ind2="2"><subfield code="u">http://www.ncbi.nlm.nih.gov/pubmed/26773485</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_USEFLAG_A</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SYSFLAG_A</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_OLC</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SSG-OLC-UMW</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SSG-OLC-TEC</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SSG-OPC-GGO</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_20</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_21</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_70</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4112</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4219</subfield></datafield><datafield tag="951" ind1=" " ind2=" "><subfield code="a">AR</subfield></datafield><datafield tag="952" ind1=" " ind2=" "><subfield code="d">91</subfield><subfield code="j">2016</subfield><subfield code="h">115-125</subfield></datafield></record></collection>
|
| author |
Floris, R |
| spellingShingle |
Floris, R ddc 550 Removal of aqueous nC60 fullerene from water by low pressure membrane filtration |
| authorStr |
Floris, R |
| ppnlink_with_tag_str_mv |
@@773@@(DE-627)129471860 |
| format |
Article |
| dewey-ones |
550 - Earth sciences |
| delete_txt_mv |
keep |
| author_role |
aut |
| collection |
OLC |
| remote_str |
false |
| illustrated |
Not Illustrated |
| issn |
0043-1354 |
| topic_title |
550 DNB Removal of aqueous nC60 fullerene from water by low pressure membrane filtration |
| topic |
ddc 550 |
| topic_unstemmed |
ddc 550 |
| topic_browse |
ddc 550 |
| format_facet |
Aufsätze Gedruckte Aufsätze |
| format_main_str_mv |
Text Zeitschrift/Artikel |
| carriertype_str_mv |
nc |
| author2_variant |
k n kn e r c er erc |
| hierarchy_parent_title |
Water research |
| hierarchy_parent_id |
129471860 |
| dewey-tens |
550 - Earth sciences & geology |
| hierarchy_top_title |
Water research |
| isfreeaccess_txt |
false |
| familylinks_str_mv |
(DE-627)129471860 (DE-600)202613-2 (DE-576)014841630 |
| title |
Removal of aqueous nC60 fullerene from water by low pressure membrane filtration |
| ctrlnum |
(DE-627)OLC1972595830 (DE-599)GBVOLC1972595830 (PRQ)c1214-a350cdae474877f5b69cbf615829540b980f5465f227db77ffd161d59f3e36590 (KEY)0018203620160000091000000115removalofaqueousnc60fullerenefromwaterbylowpressur |
| title_full |
Removal of aqueous nC60 fullerene from water by low pressure membrane filtration |
| author_sort |
Floris, R |
| journal |
Water research |
| journalStr |
Water research |
| lang_code |
eng |
| isOA_bool |
false |
| dewey-hundreds |
500 - Science |
| recordtype |
marc |
| publishDateSort |
2016 |
| contenttype_str_mv |
txt |
| container_start_page |
115 |
| author_browse |
Floris, R |
| container_volume |
91 |
| class |
550 DNB |
| format_se |
Aufsätze |
| author-letter |
Floris, R |
| doi_str_mv |
10.1016/j.watres.2015.10.014 |
| dewey-full |
550 |
| title_sort |
removal of aqueous nc60 fullerene from water by low pressure membrane filtration |
| title_auth |
Removal of aqueous nC60 fullerene from water by low pressure membrane filtration |
| abstract |
The potential environmental and health risks of engineered nanoparticles such as buckminsterfullerene C60 in water require their removal during the production of drinking water. We present a study focusing on (i) the removal mechanism and (ii) the elucidation of the role of the membrane pore size during removal of nC60 fullerene nanoparticle suspensions in dead-end microfiltration and ultrafiltration mimicking separation in real industrial water treatment plants. Membranes were selected with pore sizes ranging from 18 nm to 500 nm to determine the significance of the nC60 to membrane pore size ratio and the adsorption affinity between nC60 and membrane material during filtration. Experiments were carried out with a dead-end bench-scale system operated at constant flux conditions including a hydraulic backwash cleaning procedure. nC60 nanoparticles can be efficiently removed by low pressure membrane technology with smaller and, unexpectedly, also by mostly similar or larger pores than the particle size, although the nC60 filtration behaviour appeared to be different. The nC60 size to membrane pore size ratio and the ratio of the cake-layer deposition resistance to the clean membrane resistance, both play an important role on the nC60 filtration behaviour and on the efficiency of the backwash procedure recovering the initial membrane filtration conditions. These results become specifically significant in the context of drinking water production, for which they provide relevant information for an accurate selection between membrane processes and operational parameters for the removal of nC60 in the drinking water treatment. |
| abstractGer |
The potential environmental and health risks of engineered nanoparticles such as buckminsterfullerene C60 in water require their removal during the production of drinking water. We present a study focusing on (i) the removal mechanism and (ii) the elucidation of the role of the membrane pore size during removal of nC60 fullerene nanoparticle suspensions in dead-end microfiltration and ultrafiltration mimicking separation in real industrial water treatment plants. Membranes were selected with pore sizes ranging from 18 nm to 500 nm to determine the significance of the nC60 to membrane pore size ratio and the adsorption affinity between nC60 and membrane material during filtration. Experiments were carried out with a dead-end bench-scale system operated at constant flux conditions including a hydraulic backwash cleaning procedure. nC60 nanoparticles can be efficiently removed by low pressure membrane technology with smaller and, unexpectedly, also by mostly similar or larger pores than the particle size, although the nC60 filtration behaviour appeared to be different. The nC60 size to membrane pore size ratio and the ratio of the cake-layer deposition resistance to the clean membrane resistance, both play an important role on the nC60 filtration behaviour and on the efficiency of the backwash procedure recovering the initial membrane filtration conditions. These results become specifically significant in the context of drinking water production, for which they provide relevant information for an accurate selection between membrane processes and operational parameters for the removal of nC60 in the drinking water treatment. |
| abstract_unstemmed |
The potential environmental and health risks of engineered nanoparticles such as buckminsterfullerene C60 in water require their removal during the production of drinking water. We present a study focusing on (i) the removal mechanism and (ii) the elucidation of the role of the membrane pore size during removal of nC60 fullerene nanoparticle suspensions in dead-end microfiltration and ultrafiltration mimicking separation in real industrial water treatment plants. Membranes were selected with pore sizes ranging from 18 nm to 500 nm to determine the significance of the nC60 to membrane pore size ratio and the adsorption affinity between nC60 and membrane material during filtration. Experiments were carried out with a dead-end bench-scale system operated at constant flux conditions including a hydraulic backwash cleaning procedure. nC60 nanoparticles can be efficiently removed by low pressure membrane technology with smaller and, unexpectedly, also by mostly similar or larger pores than the particle size, although the nC60 filtration behaviour appeared to be different. The nC60 size to membrane pore size ratio and the ratio of the cake-layer deposition resistance to the clean membrane resistance, both play an important role on the nC60 filtration behaviour and on the efficiency of the backwash procedure recovering the initial membrane filtration conditions. These results become specifically significant in the context of drinking water production, for which they provide relevant information for an accurate selection between membrane processes and operational parameters for the removal of nC60 in the drinking water treatment. |
| collection_details |
GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-TEC SSG-OPC-GGO GBV_ILN_20 GBV_ILN_21 GBV_ILN_70 GBV_ILN_4112 GBV_ILN_4219 |
| title_short |
Removal of aqueous nC60 fullerene from water by low pressure membrane filtration |
| url |
http://dx.doi.org/10.1016/j.watres.2015.10.014 http://www.ncbi.nlm.nih.gov/pubmed/26773485 |
| remote_bool |
false |
| author2 |
Nijmeijer, K Cornelissen, E R |
| author2Str |
Nijmeijer, K Cornelissen, E R |
| ppnlink |
129471860 |
| mediatype_str_mv |
n |
| isOA_txt |
false |
| hochschulschrift_bool |
false |
| author2_role |
oth oth |
| doi_str |
10.1016/j.watres.2015.10.014 |
| up_date |
2024-07-03T23:45:56.065Z |
| _version_ |
1803603522163310592 |
| fullrecord_marcxml |
<?xml version="1.0" encoding="UTF-8"?><collection xmlns="http://www.loc.gov/MARC21/slim"><record><leader>01000caa a2200265 4500</leader><controlfield tag="001">OLC1972595830</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20230714183308.0</controlfield><controlfield tag="007">tu</controlfield><controlfield tag="008">160427s2016 xx ||||| 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.1016/j.watres.2015.10.014</subfield><subfield code="2">doi</subfield></datafield><datafield tag="028" ind1="5" ind2="2"><subfield code="a">PQ20160430</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)OLC1972595830</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-599)GBVOLC1972595830</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(PRQ)c1214-a350cdae474877f5b69cbf615829540b980f5465f227db77ffd161d59f3e36590</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(KEY)0018203620160000091000000115removalofaqueousnc60fullerenefromwaterbylowpressur</subfield></datafield><datafield tag="040" ind1=" " ind2=" "><subfield code="a">DE-627</subfield><subfield code="b">ger</subfield><subfield code="c">DE-627</subfield><subfield code="e">rakwb</subfield></datafield><datafield tag="041" ind1=" " ind2=" "><subfield code="a">eng</subfield></datafield><datafield tag="082" ind1="0" ind2="4"><subfield code="a">550</subfield><subfield code="q">DNB</subfield></datafield><datafield tag="100" ind1="1" ind2=" "><subfield code="a">Floris, R</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Removal of aqueous nC60 fullerene from water by low pressure membrane filtration</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2016</subfield></datafield><datafield tag="336" ind1=" " ind2=" "><subfield code="a">Text</subfield><subfield code="b">txt</subfield><subfield code="2">rdacontent</subfield></datafield><datafield tag="337" ind1=" " ind2=" "><subfield code="a">ohne Hilfsmittel zu benutzen</subfield><subfield code="b">n</subfield><subfield code="2">rdamedia</subfield></datafield><datafield tag="338" ind1=" " ind2=" "><subfield code="a">Band</subfield><subfield code="b">nc</subfield><subfield code="2">rdacarrier</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">The potential environmental and health risks of engineered nanoparticles such as buckminsterfullerene C60 in water require their removal during the production of drinking water. We present a study focusing on (i) the removal mechanism and (ii) the elucidation of the role of the membrane pore size during removal of nC60 fullerene nanoparticle suspensions in dead-end microfiltration and ultrafiltration mimicking separation in real industrial water treatment plants. Membranes were selected with pore sizes ranging from 18 nm to 500 nm to determine the significance of the nC60 to membrane pore size ratio and the adsorption affinity between nC60 and membrane material during filtration. Experiments were carried out with a dead-end bench-scale system operated at constant flux conditions including a hydraulic backwash cleaning procedure. nC60 nanoparticles can be efficiently removed by low pressure membrane technology with smaller and, unexpectedly, also by mostly similar or larger pores than the particle size, although the nC60 filtration behaviour appeared to be different. The nC60 size to membrane pore size ratio and the ratio of the cake-layer deposition resistance to the clean membrane resistance, both play an important role on the nC60 filtration behaviour and on the efficiency of the backwash procedure recovering the initial membrane filtration conditions. These results become specifically significant in the context of drinking water production, for which they provide relevant information for an accurate selection between membrane processes and operational parameters for the removal of nC60 in the drinking water treatment.</subfield></datafield><datafield tag="540" ind1=" " ind2=" "><subfield code="a">Nutzungsrecht: Copyright © 2015 Elsevier Ltd. All rights reserved.</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Nijmeijer, K</subfield><subfield code="4">oth</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Cornelissen, E R</subfield><subfield code="4">oth</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">Enthalten in</subfield><subfield code="t">Water research</subfield><subfield code="d">Amsterdam [u.a.] : Elsevier, Pergamon, 1967</subfield><subfield code="g">91(2016), Seite 115-125</subfield><subfield code="w">(DE-627)129471860</subfield><subfield code="w">(DE-600)202613-2</subfield><subfield code="w">(DE-576)014841630</subfield><subfield code="x">0043-1354</subfield><subfield code="7">nnns</subfield></datafield><datafield tag="773" ind1="1" ind2="8"><subfield code="g">volume:91</subfield><subfield code="g">year:2016</subfield><subfield code="g">pages:115-125</subfield></datafield><datafield tag="856" ind1="4" ind2="1"><subfield code="u">http://dx.doi.org/10.1016/j.watres.2015.10.014</subfield><subfield code="3">Volltext</subfield></datafield><datafield tag="856" ind1="4" ind2="2"><subfield code="u">http://www.ncbi.nlm.nih.gov/pubmed/26773485</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_USEFLAG_A</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SYSFLAG_A</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_OLC</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SSG-OLC-UMW</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SSG-OLC-TEC</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SSG-OPC-GGO</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_20</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_21</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_70</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4112</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4219</subfield></datafield><datafield tag="951" ind1=" " ind2=" "><subfield code="a">AR</subfield></datafield><datafield tag="952" ind1=" " ind2=" "><subfield code="d">91</subfield><subfield code="j">2016</subfield><subfield code="h">115-125</subfield></datafield></record></collection>
|
| score |
7.39931 |