Uranium membrane separation from binary aqueous solutions of UO
The performance of the nanofiltration process was investigated for uranium separation from binary aqueous solutions of UO 2 2+ -K + and UO 2 2+ -Ca 2+ containing uranium in high concentration ranges. Rejection coefficient, permeate flux, and membrane selectivity of PES-2, NF-1, and NF-2 membranes un...
Ausführliche Beschreibung
Autor*in: |
Ghasemi Torkabad, M [verfasserIn] |
---|
Format: |
Artikel |
---|---|
Sprache: |
Englisch |
Erschienen: |
2017 |
---|
Rechteinformationen: |
Nutzungsrecht: © 2017 Taylor & Francis 2017 |
---|
Schlagwörter: |
---|
Übergeordnetes Werk: |
Enthalten in: Separation science and technology - Philadelphia, Pa. : Taylor & Francis, 1978, 52(2017), 6, Seite 1095 |
---|---|
Übergeordnetes Werk: |
volume:52 ; year:2017 ; number:6 ; pages:1095 |
Links: |
---|
DOI / URN: |
10.1080/01496395.2017.1279182 |
---|
Katalog-ID: |
OLC1991976526 |
---|
LEADER | 01000caa a2200265 4500 | ||
---|---|---|---|
001 | OLC1991976526 | ||
003 | DE-627 | ||
005 | 20230715035906.0 | ||
007 | tu | ||
008 | 170512s2017 xx ||||| 00| ||eng c | ||
024 | 7 | |a 10.1080/01496395.2017.1279182 |2 doi | |
028 | 5 | 2 | |a PQ20170901 |
035 | |a (DE-627)OLC1991976526 | ||
035 | |a (DE-599)GBVOLC1991976526 | ||
035 | |a (PRQ)informaworld_taylorfrancis_10_1080_01496395_2017_12791820 | ||
035 | |a (KEY)0017461020170000052000601095uraniummembraneseparationfrombinaryaqueoussolution | ||
040 | |a DE-627 |b ger |c DE-627 |e rakwb | ||
041 | |a eng | ||
082 | 0 | 4 | |a 540 |q DE-600 |
100 | 1 | |a Ghasemi Torkabad, M |e verfasserin |4 aut | |
245 | 1 | 0 | |a Uranium membrane separation from binary aqueous solutions of UO |
264 | 1 | |c 2017 | |
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 performance of the nanofiltration process was investigated for uranium separation from binary aqueous solutions of UO 2 2+ -K + and UO 2 2+ -Ca 2+ containing uranium in high concentration ranges. Rejection coefficient, permeate flux, and membrane selectivity of PES-2, NF-1, and NF-2 membranes under various operational conditions of pH, pressure, and concentration of interfering cation were evaluated. In most cases, the order of metal rejections with these membranes was UO 2 2+ > Ca 2+ > K + . According to the obtained results, the nanofiltration process could be effectively used for selective uranium separation from aqueous solutions containing uranium and other monovalent and divalent cations. | ||
540 | |a Nutzungsrecht: © 2017 Taylor & Francis 2017 | ||
650 | 4 | |a nanofiltration | |
650 | 4 | |a uranium | |
650 | 4 | |a Binary aqueous solutions | |
650 | 4 | |a membrane separation | |
700 | 1 | |a Keshtkar, A. R |4 oth | |
700 | 1 | |a Safdari, S. J |4 oth | |
773 | 0 | 8 | |i Enthalten in |t Separation science and technology |d Philadelphia, Pa. : Taylor & Francis, 1978 |g 52(2017), 6, Seite 1095 |w (DE-627)12994100X |w (DE-600)391905-5 |w (DE-576)015504247 |x 0149-6395 |7 nnns |
773 | 1 | 8 | |g volume:52 |g year:2017 |g number:6 |g pages:1095 |
856 | 4 | 1 | |u http://dx.doi.org/10.1080/01496395.2017.1279182 |3 Volltext |
856 | 4 | 2 | |u http://www.tandfonline.com/doi/abs/10.1080/01496395.2017.1279182 |
912 | |a GBV_USEFLAG_A | ||
912 | |a SYSFLAG_A | ||
912 | |a GBV_OLC | ||
912 | |a SSG-OLC-TEC | ||
912 | |a SSG-OLC-CHE | ||
912 | |a SSG-OLC-PHA | ||
912 | |a SSG-OLC-DE-84 | ||
912 | |a GBV_ILN_70 | ||
951 | |a AR | ||
952 | |d 52 |j 2017 |e 6 |h 1095 |
author_variant |
t m g tm tmg |
---|---|
matchkey_str |
article:01496395:2017----::rnummrnsprtofobnrau |
hierarchy_sort_str |
2017 |
publishDate |
2017 |
allfields |
10.1080/01496395.2017.1279182 doi PQ20170901 (DE-627)OLC1991976526 (DE-599)GBVOLC1991976526 (PRQ)informaworld_taylorfrancis_10_1080_01496395_2017_12791820 (KEY)0017461020170000052000601095uraniummembraneseparationfrombinaryaqueoussolution DE-627 ger DE-627 rakwb eng 540 DE-600 Ghasemi Torkabad, M verfasserin aut Uranium membrane separation from binary aqueous solutions of UO 2017 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier The performance of the nanofiltration process was investigated for uranium separation from binary aqueous solutions of UO 2 2+ -K + and UO 2 2+ -Ca 2+ containing uranium in high concentration ranges. Rejection coefficient, permeate flux, and membrane selectivity of PES-2, NF-1, and NF-2 membranes under various operational conditions of pH, pressure, and concentration of interfering cation were evaluated. In most cases, the order of metal rejections with these membranes was UO 2 2+ > Ca 2+ > K + . According to the obtained results, the nanofiltration process could be effectively used for selective uranium separation from aqueous solutions containing uranium and other monovalent and divalent cations. Nutzungsrecht: © 2017 Taylor & Francis 2017 nanofiltration uranium Binary aqueous solutions membrane separation Keshtkar, A. R oth Safdari, S. J oth Enthalten in Separation science and technology Philadelphia, Pa. : Taylor & Francis, 1978 52(2017), 6, Seite 1095 (DE-627)12994100X (DE-600)391905-5 (DE-576)015504247 0149-6395 nnns volume:52 year:2017 number:6 pages:1095 http://dx.doi.org/10.1080/01496395.2017.1279182 Volltext http://www.tandfonline.com/doi/abs/10.1080/01496395.2017.1279182 GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 52 2017 6 1095 |
spelling |
10.1080/01496395.2017.1279182 doi PQ20170901 (DE-627)OLC1991976526 (DE-599)GBVOLC1991976526 (PRQ)informaworld_taylorfrancis_10_1080_01496395_2017_12791820 (KEY)0017461020170000052000601095uraniummembraneseparationfrombinaryaqueoussolution DE-627 ger DE-627 rakwb eng 540 DE-600 Ghasemi Torkabad, M verfasserin aut Uranium membrane separation from binary aqueous solutions of UO 2017 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier The performance of the nanofiltration process was investigated for uranium separation from binary aqueous solutions of UO 2 2+ -K + and UO 2 2+ -Ca 2+ containing uranium in high concentration ranges. Rejection coefficient, permeate flux, and membrane selectivity of PES-2, NF-1, and NF-2 membranes under various operational conditions of pH, pressure, and concentration of interfering cation were evaluated. In most cases, the order of metal rejections with these membranes was UO 2 2+ > Ca 2+ > K + . According to the obtained results, the nanofiltration process could be effectively used for selective uranium separation from aqueous solutions containing uranium and other monovalent and divalent cations. Nutzungsrecht: © 2017 Taylor & Francis 2017 nanofiltration uranium Binary aqueous solutions membrane separation Keshtkar, A. R oth Safdari, S. J oth Enthalten in Separation science and technology Philadelphia, Pa. : Taylor & Francis, 1978 52(2017), 6, Seite 1095 (DE-627)12994100X (DE-600)391905-5 (DE-576)015504247 0149-6395 nnns volume:52 year:2017 number:6 pages:1095 http://dx.doi.org/10.1080/01496395.2017.1279182 Volltext http://www.tandfonline.com/doi/abs/10.1080/01496395.2017.1279182 GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 52 2017 6 1095 |
allfields_unstemmed |
10.1080/01496395.2017.1279182 doi PQ20170901 (DE-627)OLC1991976526 (DE-599)GBVOLC1991976526 (PRQ)informaworld_taylorfrancis_10_1080_01496395_2017_12791820 (KEY)0017461020170000052000601095uraniummembraneseparationfrombinaryaqueoussolution DE-627 ger DE-627 rakwb eng 540 DE-600 Ghasemi Torkabad, M verfasserin aut Uranium membrane separation from binary aqueous solutions of UO 2017 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier The performance of the nanofiltration process was investigated for uranium separation from binary aqueous solutions of UO 2 2+ -K + and UO 2 2+ -Ca 2+ containing uranium in high concentration ranges. Rejection coefficient, permeate flux, and membrane selectivity of PES-2, NF-1, and NF-2 membranes under various operational conditions of pH, pressure, and concentration of interfering cation were evaluated. In most cases, the order of metal rejections with these membranes was UO 2 2+ > Ca 2+ > K + . According to the obtained results, the nanofiltration process could be effectively used for selective uranium separation from aqueous solutions containing uranium and other monovalent and divalent cations. Nutzungsrecht: © 2017 Taylor & Francis 2017 nanofiltration uranium Binary aqueous solutions membrane separation Keshtkar, A. R oth Safdari, S. J oth Enthalten in Separation science and technology Philadelphia, Pa. : Taylor & Francis, 1978 52(2017), 6, Seite 1095 (DE-627)12994100X (DE-600)391905-5 (DE-576)015504247 0149-6395 nnns volume:52 year:2017 number:6 pages:1095 http://dx.doi.org/10.1080/01496395.2017.1279182 Volltext http://www.tandfonline.com/doi/abs/10.1080/01496395.2017.1279182 GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 52 2017 6 1095 |
allfieldsGer |
10.1080/01496395.2017.1279182 doi PQ20170901 (DE-627)OLC1991976526 (DE-599)GBVOLC1991976526 (PRQ)informaworld_taylorfrancis_10_1080_01496395_2017_12791820 (KEY)0017461020170000052000601095uraniummembraneseparationfrombinaryaqueoussolution DE-627 ger DE-627 rakwb eng 540 DE-600 Ghasemi Torkabad, M verfasserin aut Uranium membrane separation from binary aqueous solutions of UO 2017 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier The performance of the nanofiltration process was investigated for uranium separation from binary aqueous solutions of UO 2 2+ -K + and UO 2 2+ -Ca 2+ containing uranium in high concentration ranges. Rejection coefficient, permeate flux, and membrane selectivity of PES-2, NF-1, and NF-2 membranes under various operational conditions of pH, pressure, and concentration of interfering cation were evaluated. In most cases, the order of metal rejections with these membranes was UO 2 2+ > Ca 2+ > K + . According to the obtained results, the nanofiltration process could be effectively used for selective uranium separation from aqueous solutions containing uranium and other monovalent and divalent cations. Nutzungsrecht: © 2017 Taylor & Francis 2017 nanofiltration uranium Binary aqueous solutions membrane separation Keshtkar, A. R oth Safdari, S. J oth Enthalten in Separation science and technology Philadelphia, Pa. : Taylor & Francis, 1978 52(2017), 6, Seite 1095 (DE-627)12994100X (DE-600)391905-5 (DE-576)015504247 0149-6395 nnns volume:52 year:2017 number:6 pages:1095 http://dx.doi.org/10.1080/01496395.2017.1279182 Volltext http://www.tandfonline.com/doi/abs/10.1080/01496395.2017.1279182 GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 52 2017 6 1095 |
allfieldsSound |
10.1080/01496395.2017.1279182 doi PQ20170901 (DE-627)OLC1991976526 (DE-599)GBVOLC1991976526 (PRQ)informaworld_taylorfrancis_10_1080_01496395_2017_12791820 (KEY)0017461020170000052000601095uraniummembraneseparationfrombinaryaqueoussolution DE-627 ger DE-627 rakwb eng 540 DE-600 Ghasemi Torkabad, M verfasserin aut Uranium membrane separation from binary aqueous solutions of UO 2017 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier The performance of the nanofiltration process was investigated for uranium separation from binary aqueous solutions of UO 2 2+ -K + and UO 2 2+ -Ca 2+ containing uranium in high concentration ranges. Rejection coefficient, permeate flux, and membrane selectivity of PES-2, NF-1, and NF-2 membranes under various operational conditions of pH, pressure, and concentration of interfering cation were evaluated. In most cases, the order of metal rejections with these membranes was UO 2 2+ > Ca 2+ > K + . According to the obtained results, the nanofiltration process could be effectively used for selective uranium separation from aqueous solutions containing uranium and other monovalent and divalent cations. Nutzungsrecht: © 2017 Taylor & Francis 2017 nanofiltration uranium Binary aqueous solutions membrane separation Keshtkar, A. R oth Safdari, S. J oth Enthalten in Separation science and technology Philadelphia, Pa. : Taylor & Francis, 1978 52(2017), 6, Seite 1095 (DE-627)12994100X (DE-600)391905-5 (DE-576)015504247 0149-6395 nnns volume:52 year:2017 number:6 pages:1095 http://dx.doi.org/10.1080/01496395.2017.1279182 Volltext http://www.tandfonline.com/doi/abs/10.1080/01496395.2017.1279182 GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 52 2017 6 1095 |
language |
English |
source |
Enthalten in Separation science and technology 52(2017), 6, Seite 1095 volume:52 year:2017 number:6 pages:1095 |
sourceStr |
Enthalten in Separation science and technology 52(2017), 6, Seite 1095 volume:52 year:2017 number:6 pages:1095 |
format_phy_str_mv |
Article |
institution |
findex.gbv.de |
topic_facet |
nanofiltration uranium Binary aqueous solutions membrane separation |
dewey-raw |
540 |
isfreeaccess_bool |
false |
container_title |
Separation science and technology |
authorswithroles_txt_mv |
Ghasemi Torkabad, M @@aut@@ Keshtkar, A. R @@oth@@ Safdari, S. J @@oth@@ |
publishDateDaySort_date |
2017-01-01T00:00:00Z |
hierarchy_top_id |
12994100X |
dewey-sort |
3540 |
id |
OLC1991976526 |
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">OLC1991976526</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20230715035906.0</controlfield><controlfield tag="007">tu</controlfield><controlfield tag="008">170512s2017 xx ||||| 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.1080/01496395.2017.1279182</subfield><subfield code="2">doi</subfield></datafield><datafield tag="028" ind1="5" ind2="2"><subfield code="a">PQ20170901</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)OLC1991976526</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-599)GBVOLC1991976526</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(PRQ)informaworld_taylorfrancis_10_1080_01496395_2017_12791820</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(KEY)0017461020170000052000601095uraniummembraneseparationfrombinaryaqueoussolution</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">540</subfield><subfield code="q">DE-600</subfield></datafield><datafield tag="100" ind1="1" ind2=" "><subfield code="a">Ghasemi Torkabad, M</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Uranium membrane separation from binary aqueous solutions of UO</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2017</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 performance of the nanofiltration process was investigated for uranium separation from binary aqueous solutions of UO 2 2+ -K + and UO 2 2+ -Ca 2+ containing uranium in high concentration ranges. Rejection coefficient, permeate flux, and membrane selectivity of PES-2, NF-1, and NF-2 membranes under various operational conditions of pH, pressure, and concentration of interfering cation were evaluated. In most cases, the order of metal rejections with these membranes was UO 2 2+ > Ca 2+ > K + . According to the obtained results, the nanofiltration process could be effectively used for selective uranium separation from aqueous solutions containing uranium and other monovalent and divalent cations.</subfield></datafield><datafield tag="540" ind1=" " ind2=" "><subfield code="a">Nutzungsrecht: © 2017 Taylor & Francis 2017</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">nanofiltration</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">uranium</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Binary aqueous solutions</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">membrane separation</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Keshtkar, A. R</subfield><subfield code="4">oth</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Safdari, S. J</subfield><subfield code="4">oth</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">Enthalten in</subfield><subfield code="t">Separation science and technology</subfield><subfield code="d">Philadelphia, Pa. : Taylor & Francis, 1978</subfield><subfield code="g">52(2017), 6, Seite 1095</subfield><subfield code="w">(DE-627)12994100X</subfield><subfield code="w">(DE-600)391905-5</subfield><subfield code="w">(DE-576)015504247</subfield><subfield code="x">0149-6395</subfield><subfield code="7">nnns</subfield></datafield><datafield tag="773" ind1="1" ind2="8"><subfield code="g">volume:52</subfield><subfield code="g">year:2017</subfield><subfield code="g">number:6</subfield><subfield code="g">pages:1095</subfield></datafield><datafield tag="856" ind1="4" ind2="1"><subfield code="u">http://dx.doi.org/10.1080/01496395.2017.1279182</subfield><subfield code="3">Volltext</subfield></datafield><datafield tag="856" ind1="4" ind2="2"><subfield code="u">http://www.tandfonline.com/doi/abs/10.1080/01496395.2017.1279182</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-TEC</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SSG-OLC-CHE</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SSG-OLC-PHA</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SSG-OLC-DE-84</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_70</subfield></datafield><datafield tag="951" ind1=" " ind2=" "><subfield code="a">AR</subfield></datafield><datafield tag="952" ind1=" " ind2=" "><subfield code="d">52</subfield><subfield code="j">2017</subfield><subfield code="e">6</subfield><subfield code="h">1095</subfield></datafield></record></collection>
|
author |
Ghasemi Torkabad, M |
spellingShingle |
Ghasemi Torkabad, M ddc 540 misc nanofiltration misc uranium misc Binary aqueous solutions misc membrane separation Uranium membrane separation from binary aqueous solutions of UO |
authorStr |
Ghasemi Torkabad, M |
ppnlink_with_tag_str_mv |
@@773@@(DE-627)12994100X |
format |
Article |
dewey-ones |
540 - Chemistry & allied sciences |
delete_txt_mv |
keep |
author_role |
aut |
collection |
OLC |
remote_str |
false |
illustrated |
Not Illustrated |
issn |
0149-6395 |
topic_title |
540 DE-600 Uranium membrane separation from binary aqueous solutions of UO nanofiltration uranium Binary aqueous solutions membrane separation |
topic |
ddc 540 misc nanofiltration misc uranium misc Binary aqueous solutions misc membrane separation |
topic_unstemmed |
ddc 540 misc nanofiltration misc uranium misc Binary aqueous solutions misc membrane separation |
topic_browse |
ddc 540 misc nanofiltration misc uranium misc Binary aqueous solutions misc membrane separation |
format_facet |
Aufsätze Gedruckte Aufsätze |
format_main_str_mv |
Text Zeitschrift/Artikel |
carriertype_str_mv |
nc |
author2_variant |
a r k ar ark s j s sj sjs |
hierarchy_parent_title |
Separation science and technology |
hierarchy_parent_id |
12994100X |
dewey-tens |
540 - Chemistry |
hierarchy_top_title |
Separation science and technology |
isfreeaccess_txt |
false |
familylinks_str_mv |
(DE-627)12994100X (DE-600)391905-5 (DE-576)015504247 |
title |
Uranium membrane separation from binary aqueous solutions of UO |
ctrlnum |
(DE-627)OLC1991976526 (DE-599)GBVOLC1991976526 (PRQ)informaworld_taylorfrancis_10_1080_01496395_2017_12791820 (KEY)0017461020170000052000601095uraniummembraneseparationfrombinaryaqueoussolution |
title_full |
Uranium membrane separation from binary aqueous solutions of UO |
author_sort |
Ghasemi Torkabad, M |
journal |
Separation science and technology |
journalStr |
Separation science and technology |
lang_code |
eng |
isOA_bool |
false |
dewey-hundreds |
500 - Science |
recordtype |
marc |
publishDateSort |
2017 |
contenttype_str_mv |
txt |
container_start_page |
1095 |
author_browse |
Ghasemi Torkabad, M |
container_volume |
52 |
class |
540 DE-600 |
format_se |
Aufsätze |
author-letter |
Ghasemi Torkabad, M |
doi_str_mv |
10.1080/01496395.2017.1279182 |
dewey-full |
540 |
title_sort |
uranium membrane separation from binary aqueous solutions of uo |
title_auth |
Uranium membrane separation from binary aqueous solutions of UO |
abstract |
The performance of the nanofiltration process was investigated for uranium separation from binary aqueous solutions of UO 2 2+ -K + and UO 2 2+ -Ca 2+ containing uranium in high concentration ranges. Rejection coefficient, permeate flux, and membrane selectivity of PES-2, NF-1, and NF-2 membranes under various operational conditions of pH, pressure, and concentration of interfering cation were evaluated. In most cases, the order of metal rejections with these membranes was UO 2 2+ > Ca 2+ > K + . According to the obtained results, the nanofiltration process could be effectively used for selective uranium separation from aqueous solutions containing uranium and other monovalent and divalent cations. |
abstractGer |
The performance of the nanofiltration process was investigated for uranium separation from binary aqueous solutions of UO 2 2+ -K + and UO 2 2+ -Ca 2+ containing uranium in high concentration ranges. Rejection coefficient, permeate flux, and membrane selectivity of PES-2, NF-1, and NF-2 membranes under various operational conditions of pH, pressure, and concentration of interfering cation were evaluated. In most cases, the order of metal rejections with these membranes was UO 2 2+ > Ca 2+ > K + . According to the obtained results, the nanofiltration process could be effectively used for selective uranium separation from aqueous solutions containing uranium and other monovalent and divalent cations. |
abstract_unstemmed |
The performance of the nanofiltration process was investigated for uranium separation from binary aqueous solutions of UO 2 2+ -K + and UO 2 2+ -Ca 2+ containing uranium in high concentration ranges. Rejection coefficient, permeate flux, and membrane selectivity of PES-2, NF-1, and NF-2 membranes under various operational conditions of pH, pressure, and concentration of interfering cation were evaluated. In most cases, the order of metal rejections with these membranes was UO 2 2+ > Ca 2+ > K + . According to the obtained results, the nanofiltration process could be effectively used for selective uranium separation from aqueous solutions containing uranium and other monovalent and divalent cations. |
collection_details |
GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 |
container_issue |
6 |
title_short |
Uranium membrane separation from binary aqueous solutions of UO |
url |
http://dx.doi.org/10.1080/01496395.2017.1279182 http://www.tandfonline.com/doi/abs/10.1080/01496395.2017.1279182 |
remote_bool |
false |
author2 |
Keshtkar, A. R Safdari, S. J |
author2Str |
Keshtkar, A. R Safdari, S. J |
ppnlink |
12994100X |
mediatype_str_mv |
n |
isOA_txt |
false |
hochschulschrift_bool |
false |
author2_role |
oth oth |
doi_str |
10.1080/01496395.2017.1279182 |
up_date |
2024-07-04T04:00:51.185Z |
_version_ |
1803619560258011136 |
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">OLC1991976526</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20230715035906.0</controlfield><controlfield tag="007">tu</controlfield><controlfield tag="008">170512s2017 xx ||||| 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.1080/01496395.2017.1279182</subfield><subfield code="2">doi</subfield></datafield><datafield tag="028" ind1="5" ind2="2"><subfield code="a">PQ20170901</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)OLC1991976526</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-599)GBVOLC1991976526</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(PRQ)informaworld_taylorfrancis_10_1080_01496395_2017_12791820</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(KEY)0017461020170000052000601095uraniummembraneseparationfrombinaryaqueoussolution</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">540</subfield><subfield code="q">DE-600</subfield></datafield><datafield tag="100" ind1="1" ind2=" "><subfield code="a">Ghasemi Torkabad, M</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Uranium membrane separation from binary aqueous solutions of UO</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2017</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 performance of the nanofiltration process was investigated for uranium separation from binary aqueous solutions of UO 2 2+ -K + and UO 2 2+ -Ca 2+ containing uranium in high concentration ranges. Rejection coefficient, permeate flux, and membrane selectivity of PES-2, NF-1, and NF-2 membranes under various operational conditions of pH, pressure, and concentration of interfering cation were evaluated. In most cases, the order of metal rejections with these membranes was UO 2 2+ > Ca 2+ > K + . According to the obtained results, the nanofiltration process could be effectively used for selective uranium separation from aqueous solutions containing uranium and other monovalent and divalent cations.</subfield></datafield><datafield tag="540" ind1=" " ind2=" "><subfield code="a">Nutzungsrecht: © 2017 Taylor & Francis 2017</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">nanofiltration</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">uranium</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Binary aqueous solutions</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">membrane separation</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Keshtkar, A. R</subfield><subfield code="4">oth</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Safdari, S. J</subfield><subfield code="4">oth</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">Enthalten in</subfield><subfield code="t">Separation science and technology</subfield><subfield code="d">Philadelphia, Pa. : Taylor & Francis, 1978</subfield><subfield code="g">52(2017), 6, Seite 1095</subfield><subfield code="w">(DE-627)12994100X</subfield><subfield code="w">(DE-600)391905-5</subfield><subfield code="w">(DE-576)015504247</subfield><subfield code="x">0149-6395</subfield><subfield code="7">nnns</subfield></datafield><datafield tag="773" ind1="1" ind2="8"><subfield code="g">volume:52</subfield><subfield code="g">year:2017</subfield><subfield code="g">number:6</subfield><subfield code="g">pages:1095</subfield></datafield><datafield tag="856" ind1="4" ind2="1"><subfield code="u">http://dx.doi.org/10.1080/01496395.2017.1279182</subfield><subfield code="3">Volltext</subfield></datafield><datafield tag="856" ind1="4" ind2="2"><subfield code="u">http://www.tandfonline.com/doi/abs/10.1080/01496395.2017.1279182</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-TEC</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SSG-OLC-CHE</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SSG-OLC-PHA</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">SSG-OLC-DE-84</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_70</subfield></datafield><datafield tag="951" ind1=" " ind2=" "><subfield code="a">AR</subfield></datafield><datafield tag="952" ind1=" " ind2=" "><subfield code="d">52</subfield><subfield code="j">2017</subfield><subfield code="e">6</subfield><subfield code="h">1095</subfield></datafield></record></collection>
|
score |
7.401577 |