Recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions via membrane distillation
Abstract The simultaneous recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions by air gap membrane distillation was theoretically assessed. A previously developed and validated Stefan–Maxwell based mathematical model was used for this purpose. It was found that membrane d...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Banat, F. A. [verfasserIn] |
|---|
| Format: |
Artikel |
|---|---|
| Sprache: |
Englisch |
| Erschienen: |
2000 |
|---|
| Schlagwörter: |
|---|
| Anmerkung: |
© Springer-Verlag Berlin Heidelberg 2000 |
|---|
| Übergeordnetes Werk: |
Enthalten in: Bioprocess engineering - Springer-Verlag, 1986, 23(2000), 6 vom: Dez., Seite 643-649 |
|---|---|
| Übergeordnetes Werk: |
volume:23 ; year:2000 ; number:6 ; month:12 ; pages:643-649 |
| Links: |
|---|
| DOI / URN: |
10.1007/s004490000214 |
|---|
| Katalog-ID: |
OLC2106607024 |
|---|
| LEADER | 01000naa a22002652 4500 | ||
|---|---|---|---|
| 001 | OLC2106607024 | ||
| 003 | DE-627 | ||
| 005 | 20230403073213.0 | ||
| 007 | tu | ||
| 008 | 230403s2000 xx ||||| 00| ||eng c | ||
| 024 | 7 | |a 10.1007/s004490000214 |2 doi | |
| 035 | |a (DE-627)OLC2106607024 | ||
| 035 | |a (DE-He213)s004490000214-p | ||
| 040 | |a DE-627 |b ger |c DE-627 |e rakwb | ||
| 041 | |a eng | ||
| 082 | 0 | 4 | |a 570 |a 690 |a 540 |q VZ |
| 084 | |a 12 |2 ssgn | ||
| 100 | 1 | |a Banat, F. A. |e verfasserin |4 aut | |
| 245 | 1 | 0 | |a Recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions via membrane distillation |
| 264 | 1 | |c 2000 | |
| 336 | |a Text |b txt |2 rdacontent | ||
| 337 | |a ohne Hilfsmittel zu benutzen |b n |2 rdamedia | ||
| 338 | |a Band |b nc |2 rdacarrier | ||
| 500 | |a © Springer-Verlag Berlin Heidelberg 2000 | ||
| 520 | |a Abstract The simultaneous recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions by air gap membrane distillation was theoretically assessed. A previously developed and validated Stefan–Maxwell based mathematical model was used for this purpose. It was found that membrane distillation could successfully be used for the recovery of these solvents. Interestingly it was found that butanol could be separated with the highest selectivity and flux though it has the highest boiling point. The effect of operating conditions such as feed and cooling surface temperatures, air gap width, and individual component concentration on the flux and selectivity of these solvents was examined and discussed in this paper. | ||
| 650 | 4 | |a Aqueous Solution | |
| 650 | 4 | |a Acetone | |
| 650 | 4 | |a Surface Temperature | |
| 650 | 4 | |a Boiling | |
| 650 | 4 | |a Butanol | |
| 700 | 1 | |a Al-Shannag, M. |4 aut | |
| 773 | 0 | 8 | |i Enthalten in |t Bioprocess engineering |d Springer-Verlag, 1986 |g 23(2000), 6 vom: Dez., Seite 643-649 |w (DE-627)129208922 |w (DE-600)55154-5 |w (DE-576)01445761X |x 0178-515X |7 nnns |
| 773 | 1 | 8 | |g volume:23 |g year:2000 |g number:6 |g month:12 |g pages:643-649 |
| 856 | 4 | 1 | |u https://doi.org/10.1007/s004490000214 |z lizenzpflichtig |3 Volltext |
| 912 | |a GBV_USEFLAG_A | ||
| 912 | |a SYSFLAG_A | ||
| 912 | |a GBV_OLC | ||
| 912 | |a SSG-OLC-UMW | ||
| 912 | |a SSG-OLC-ARC | ||
| 912 | |a SSG-OLC-TEC | ||
| 912 | |a SSG-OLC-CHE | ||
| 912 | |a GBV_ILN_11 | ||
| 912 | |a GBV_ILN_23 | ||
| 912 | |a GBV_ILN_32 | ||
| 912 | |a GBV_ILN_40 | ||
| 912 | |a GBV_ILN_65 | ||
| 912 | |a GBV_ILN_70 | ||
| 912 | |a GBV_ILN_2006 | ||
| 912 | |a GBV_ILN_2018 | ||
| 912 | |a GBV_ILN_4046 | ||
| 912 | |a GBV_ILN_4277 | ||
| 912 | |a GBV_ILN_4307 | ||
| 912 | |a GBV_ILN_4310 | ||
| 912 | |a GBV_ILN_4328 | ||
| 951 | |a AR | ||
| 952 | |d 23 |j 2000 |e 6 |c 12 |h 643-649 | ||
| author_variant |
f a b fa fab m a s mas |
|---|---|
| matchkey_str |
article:0178515X:2000----::eoeyfiuectnbtnltaoaeovnsrmqeuslto |
| hierarchy_sort_str |
2000 |
| publishDate |
2000 |
| allfields |
10.1007/s004490000214 doi (DE-627)OLC2106607024 (DE-He213)s004490000214-p DE-627 ger DE-627 rakwb eng 570 690 540 VZ 12 ssgn Banat, F. A. verfasserin aut Recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions via membrane distillation 2000 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Springer-Verlag Berlin Heidelberg 2000 Abstract The simultaneous recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions by air gap membrane distillation was theoretically assessed. A previously developed and validated Stefan–Maxwell based mathematical model was used for this purpose. It was found that membrane distillation could successfully be used for the recovery of these solvents. Interestingly it was found that butanol could be separated with the highest selectivity and flux though it has the highest boiling point. The effect of operating conditions such as feed and cooling surface temperatures, air gap width, and individual component concentration on the flux and selectivity of these solvents was examined and discussed in this paper. Aqueous Solution Acetone Surface Temperature Boiling Butanol Al-Shannag, M. aut Enthalten in Bioprocess engineering Springer-Verlag, 1986 23(2000), 6 vom: Dez., Seite 643-649 (DE-627)129208922 (DE-600)55154-5 (DE-576)01445761X 0178-515X nnns volume:23 year:2000 number:6 month:12 pages:643-649 https://doi.org/10.1007/s004490000214 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-CHE GBV_ILN_11 GBV_ILN_23 GBV_ILN_32 GBV_ILN_40 GBV_ILN_65 GBV_ILN_70 GBV_ILN_2006 GBV_ILN_2018 GBV_ILN_4046 GBV_ILN_4277 GBV_ILN_4307 GBV_ILN_4310 GBV_ILN_4328 AR 23 2000 6 12 643-649 |
| spelling |
10.1007/s004490000214 doi (DE-627)OLC2106607024 (DE-He213)s004490000214-p DE-627 ger DE-627 rakwb eng 570 690 540 VZ 12 ssgn Banat, F. A. verfasserin aut Recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions via membrane distillation 2000 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Springer-Verlag Berlin Heidelberg 2000 Abstract The simultaneous recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions by air gap membrane distillation was theoretically assessed. A previously developed and validated Stefan–Maxwell based mathematical model was used for this purpose. It was found that membrane distillation could successfully be used for the recovery of these solvents. Interestingly it was found that butanol could be separated with the highest selectivity and flux though it has the highest boiling point. The effect of operating conditions such as feed and cooling surface temperatures, air gap width, and individual component concentration on the flux and selectivity of these solvents was examined and discussed in this paper. Aqueous Solution Acetone Surface Temperature Boiling Butanol Al-Shannag, M. aut Enthalten in Bioprocess engineering Springer-Verlag, 1986 23(2000), 6 vom: Dez., Seite 643-649 (DE-627)129208922 (DE-600)55154-5 (DE-576)01445761X 0178-515X nnns volume:23 year:2000 number:6 month:12 pages:643-649 https://doi.org/10.1007/s004490000214 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-CHE GBV_ILN_11 GBV_ILN_23 GBV_ILN_32 GBV_ILN_40 GBV_ILN_65 GBV_ILN_70 GBV_ILN_2006 GBV_ILN_2018 GBV_ILN_4046 GBV_ILN_4277 GBV_ILN_4307 GBV_ILN_4310 GBV_ILN_4328 AR 23 2000 6 12 643-649 |
| allfields_unstemmed |
10.1007/s004490000214 doi (DE-627)OLC2106607024 (DE-He213)s004490000214-p DE-627 ger DE-627 rakwb eng 570 690 540 VZ 12 ssgn Banat, F. A. verfasserin aut Recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions via membrane distillation 2000 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Springer-Verlag Berlin Heidelberg 2000 Abstract The simultaneous recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions by air gap membrane distillation was theoretically assessed. A previously developed and validated Stefan–Maxwell based mathematical model was used for this purpose. It was found that membrane distillation could successfully be used for the recovery of these solvents. Interestingly it was found that butanol could be separated with the highest selectivity and flux though it has the highest boiling point. The effect of operating conditions such as feed and cooling surface temperatures, air gap width, and individual component concentration on the flux and selectivity of these solvents was examined and discussed in this paper. Aqueous Solution Acetone Surface Temperature Boiling Butanol Al-Shannag, M. aut Enthalten in Bioprocess engineering Springer-Verlag, 1986 23(2000), 6 vom: Dez., Seite 643-649 (DE-627)129208922 (DE-600)55154-5 (DE-576)01445761X 0178-515X nnns volume:23 year:2000 number:6 month:12 pages:643-649 https://doi.org/10.1007/s004490000214 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-CHE GBV_ILN_11 GBV_ILN_23 GBV_ILN_32 GBV_ILN_40 GBV_ILN_65 GBV_ILN_70 GBV_ILN_2006 GBV_ILN_2018 GBV_ILN_4046 GBV_ILN_4277 GBV_ILN_4307 GBV_ILN_4310 GBV_ILN_4328 AR 23 2000 6 12 643-649 |
| allfieldsGer |
10.1007/s004490000214 doi (DE-627)OLC2106607024 (DE-He213)s004490000214-p DE-627 ger DE-627 rakwb eng 570 690 540 VZ 12 ssgn Banat, F. A. verfasserin aut Recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions via membrane distillation 2000 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Springer-Verlag Berlin Heidelberg 2000 Abstract The simultaneous recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions by air gap membrane distillation was theoretically assessed. A previously developed and validated Stefan–Maxwell based mathematical model was used for this purpose. It was found that membrane distillation could successfully be used for the recovery of these solvents. Interestingly it was found that butanol could be separated with the highest selectivity and flux though it has the highest boiling point. The effect of operating conditions such as feed and cooling surface temperatures, air gap width, and individual component concentration on the flux and selectivity of these solvents was examined and discussed in this paper. Aqueous Solution Acetone Surface Temperature Boiling Butanol Al-Shannag, M. aut Enthalten in Bioprocess engineering Springer-Verlag, 1986 23(2000), 6 vom: Dez., Seite 643-649 (DE-627)129208922 (DE-600)55154-5 (DE-576)01445761X 0178-515X nnns volume:23 year:2000 number:6 month:12 pages:643-649 https://doi.org/10.1007/s004490000214 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-CHE GBV_ILN_11 GBV_ILN_23 GBV_ILN_32 GBV_ILN_40 GBV_ILN_65 GBV_ILN_70 GBV_ILN_2006 GBV_ILN_2018 GBV_ILN_4046 GBV_ILN_4277 GBV_ILN_4307 GBV_ILN_4310 GBV_ILN_4328 AR 23 2000 6 12 643-649 |
| allfieldsSound |
10.1007/s004490000214 doi (DE-627)OLC2106607024 (DE-He213)s004490000214-p DE-627 ger DE-627 rakwb eng 570 690 540 VZ 12 ssgn Banat, F. A. verfasserin aut Recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions via membrane distillation 2000 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Springer-Verlag Berlin Heidelberg 2000 Abstract The simultaneous recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions by air gap membrane distillation was theoretically assessed. A previously developed and validated Stefan–Maxwell based mathematical model was used for this purpose. It was found that membrane distillation could successfully be used for the recovery of these solvents. Interestingly it was found that butanol could be separated with the highest selectivity and flux though it has the highest boiling point. The effect of operating conditions such as feed and cooling surface temperatures, air gap width, and individual component concentration on the flux and selectivity of these solvents was examined and discussed in this paper. Aqueous Solution Acetone Surface Temperature Boiling Butanol Al-Shannag, M. aut Enthalten in Bioprocess engineering Springer-Verlag, 1986 23(2000), 6 vom: Dez., Seite 643-649 (DE-627)129208922 (DE-600)55154-5 (DE-576)01445761X 0178-515X nnns volume:23 year:2000 number:6 month:12 pages:643-649 https://doi.org/10.1007/s004490000214 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-CHE GBV_ILN_11 GBV_ILN_23 GBV_ILN_32 GBV_ILN_40 GBV_ILN_65 GBV_ILN_70 GBV_ILN_2006 GBV_ILN_2018 GBV_ILN_4046 GBV_ILN_4277 GBV_ILN_4307 GBV_ILN_4310 GBV_ILN_4328 AR 23 2000 6 12 643-649 |
| language |
English |
| source |
Enthalten in Bioprocess engineering 23(2000), 6 vom: Dez., Seite 643-649 volume:23 year:2000 number:6 month:12 pages:643-649 |
| sourceStr |
Enthalten in Bioprocess engineering 23(2000), 6 vom: Dez., Seite 643-649 volume:23 year:2000 number:6 month:12 pages:643-649 |
| format_phy_str_mv |
Article |
| institution |
findex.gbv.de |
| topic_facet |
Aqueous Solution Acetone Surface Temperature Boiling Butanol |
| dewey-raw |
570 |
| isfreeaccess_bool |
false |
| container_title |
Bioprocess engineering |
| authorswithroles_txt_mv |
Banat, F. A. @@aut@@ Al-Shannag, M. @@aut@@ |
| publishDateDaySort_date |
2000-12-01T00:00:00Z |
| hierarchy_top_id |
129208922 |
| dewey-sort |
3570 |
| id |
OLC2106607024 |
| language_de |
englisch |
| fullrecord |
<?xml version="1.0" encoding="UTF-8"?><collection xmlns="http://www.loc.gov/MARC21/slim"><record><leader>01000naa a22002652 4500</leader><controlfield tag="001">OLC2106607024</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20230403073213.0</controlfield><controlfield tag="007">tu</controlfield><controlfield tag="008">230403s2000 xx ||||| 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.1007/s004490000214</subfield><subfield code="2">doi</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)OLC2106607024</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-He213)s004490000214-p</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">570</subfield><subfield code="a">690</subfield><subfield code="a">540</subfield><subfield code="q">VZ</subfield></datafield><datafield tag="084" ind1=" " ind2=" "><subfield code="a">12</subfield><subfield code="2">ssgn</subfield></datafield><datafield tag="100" ind1="1" ind2=" "><subfield code="a">Banat, F. A.</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions via membrane distillation</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2000</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="500" ind1=" " ind2=" "><subfield code="a">© Springer-Verlag Berlin Heidelberg 2000</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Abstract The simultaneous recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions by air gap membrane distillation was theoretically assessed. A previously developed and validated Stefan–Maxwell based mathematical model was used for this purpose. It was found that membrane distillation could successfully be used for the recovery of these solvents. Interestingly it was found that butanol could be separated with the highest selectivity and flux though it has the highest boiling point. The effect of operating conditions such as feed and cooling surface temperatures, air gap width, and individual component concentration on the flux and selectivity of these solvents was examined and discussed in this paper.</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Aqueous Solution</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Acetone</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Surface Temperature</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Boiling</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Butanol</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Al-Shannag, M.</subfield><subfield code="4">aut</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">Enthalten in</subfield><subfield code="t">Bioprocess engineering</subfield><subfield code="d">Springer-Verlag, 1986</subfield><subfield code="g">23(2000), 6 vom: Dez., Seite 643-649</subfield><subfield code="w">(DE-627)129208922</subfield><subfield code="w">(DE-600)55154-5</subfield><subfield code="w">(DE-576)01445761X</subfield><subfield code="x">0178-515X</subfield><subfield code="7">nnns</subfield></datafield><datafield tag="773" ind1="1" ind2="8"><subfield code="g">volume:23</subfield><subfield code="g">year:2000</subfield><subfield code="g">number:6</subfield><subfield code="g">month:12</subfield><subfield code="g">pages:643-649</subfield></datafield><datafield tag="856" ind1="4" ind2="1"><subfield code="u">https://doi.org/10.1007/s004490000214</subfield><subfield code="z">lizenzpflichtig</subfield><subfield code="3">Volltext</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-ARC</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">GBV_ILN_11</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_23</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_32</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_40</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_65</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_2006</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_2018</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4046</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4277</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4307</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4310</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4328</subfield></datafield><datafield tag="951" ind1=" " ind2=" "><subfield code="a">AR</subfield></datafield><datafield tag="952" ind1=" " ind2=" "><subfield code="d">23</subfield><subfield code="j">2000</subfield><subfield code="e">6</subfield><subfield code="c">12</subfield><subfield code="h">643-649</subfield></datafield></record></collection>
|
| author |
Banat, F. A. |
| spellingShingle |
Banat, F. A. ddc 570 ssgn 12 misc Aqueous Solution misc Acetone misc Surface Temperature misc Boiling misc Butanol Recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions via membrane distillation |
| authorStr |
Banat, F. A. |
| ppnlink_with_tag_str_mv |
@@773@@(DE-627)129208922 |
| format |
Article |
| dewey-ones |
570 - Life sciences; biology 690 - Buildings 540 - Chemistry & allied sciences |
| delete_txt_mv |
keep |
| author_role |
aut aut |
| collection |
OLC |
| remote_str |
false |
| illustrated |
Not Illustrated |
| issn |
0178-515X |
| topic_title |
570 690 540 VZ 12 ssgn Recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions via membrane distillation Aqueous Solution Acetone Surface Temperature Boiling Butanol |
| topic |
ddc 570 ssgn 12 misc Aqueous Solution misc Acetone misc Surface Temperature misc Boiling misc Butanol |
| topic_unstemmed |
ddc 570 ssgn 12 misc Aqueous Solution misc Acetone misc Surface Temperature misc Boiling misc Butanol |
| topic_browse |
ddc 570 ssgn 12 misc Aqueous Solution misc Acetone misc Surface Temperature misc Boiling misc Butanol |
| format_facet |
Aufsätze Gedruckte Aufsätze |
| format_main_str_mv |
Text Zeitschrift/Artikel |
| carriertype_str_mv |
nc |
| hierarchy_parent_title |
Bioprocess engineering |
| hierarchy_parent_id |
129208922 |
| dewey-tens |
570 - Life sciences; biology 690 - Building & construction 540 - Chemistry |
| hierarchy_top_title |
Bioprocess engineering |
| isfreeaccess_txt |
false |
| familylinks_str_mv |
(DE-627)129208922 (DE-600)55154-5 (DE-576)01445761X |
| title |
Recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions via membrane distillation |
| ctrlnum |
(DE-627)OLC2106607024 (DE-He213)s004490000214-p |
| title_full |
Recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions via membrane distillation |
| author_sort |
Banat, F. A. |
| journal |
Bioprocess engineering |
| journalStr |
Bioprocess engineering |
| lang_code |
eng |
| isOA_bool |
false |
| dewey-hundreds |
500 - Science 600 - Technology |
| recordtype |
marc |
| publishDateSort |
2000 |
| contenttype_str_mv |
txt |
| container_start_page |
643 |
| author_browse |
Banat, F. A. Al-Shannag, M. |
| container_volume |
23 |
| class |
570 690 540 VZ 12 ssgn |
| format_se |
Aufsätze |
| author-letter |
Banat, F. A. |
| doi_str_mv |
10.1007/s004490000214 |
| dewey-full |
570 690 540 |
| title_sort |
recovery of dilute acetone–butanol–ethanol (abe) solvents from aqueous solutions via membrane distillation |
| title_auth |
Recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions via membrane distillation |
| abstract |
Abstract The simultaneous recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions by air gap membrane distillation was theoretically assessed. A previously developed and validated Stefan–Maxwell based mathematical model was used for this purpose. It was found that membrane distillation could successfully be used for the recovery of these solvents. Interestingly it was found that butanol could be separated with the highest selectivity and flux though it has the highest boiling point. The effect of operating conditions such as feed and cooling surface temperatures, air gap width, and individual component concentration on the flux and selectivity of these solvents was examined and discussed in this paper. © Springer-Verlag Berlin Heidelberg 2000 |
| abstractGer |
Abstract The simultaneous recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions by air gap membrane distillation was theoretically assessed. A previously developed and validated Stefan–Maxwell based mathematical model was used for this purpose. It was found that membrane distillation could successfully be used for the recovery of these solvents. Interestingly it was found that butanol could be separated with the highest selectivity and flux though it has the highest boiling point. The effect of operating conditions such as feed and cooling surface temperatures, air gap width, and individual component concentration on the flux and selectivity of these solvents was examined and discussed in this paper. © Springer-Verlag Berlin Heidelberg 2000 |
| abstract_unstemmed |
Abstract The simultaneous recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions by air gap membrane distillation was theoretically assessed. A previously developed and validated Stefan–Maxwell based mathematical model was used for this purpose. It was found that membrane distillation could successfully be used for the recovery of these solvents. Interestingly it was found that butanol could be separated with the highest selectivity and flux though it has the highest boiling point. The effect of operating conditions such as feed and cooling surface temperatures, air gap width, and individual component concentration on the flux and selectivity of these solvents was examined and discussed in this paper. © Springer-Verlag Berlin Heidelberg 2000 |
| collection_details |
GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-CHE GBV_ILN_11 GBV_ILN_23 GBV_ILN_32 GBV_ILN_40 GBV_ILN_65 GBV_ILN_70 GBV_ILN_2006 GBV_ILN_2018 GBV_ILN_4046 GBV_ILN_4277 GBV_ILN_4307 GBV_ILN_4310 GBV_ILN_4328 |
| container_issue |
6 |
| title_short |
Recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions via membrane distillation |
| url |
https://doi.org/10.1007/s004490000214 |
| remote_bool |
false |
| author2 |
Al-Shannag, M. |
| author2Str |
Al-Shannag, M. |
| ppnlink |
129208922 |
| mediatype_str_mv |
n |
| isOA_txt |
false |
| hochschulschrift_bool |
false |
| doi_str |
10.1007/s004490000214 |
| up_date |
2024-07-04T07:04:36.715Z |
| _version_ |
1803631121364156416 |
| fullrecord_marcxml |
<?xml version="1.0" encoding="UTF-8"?><collection xmlns="http://www.loc.gov/MARC21/slim"><record><leader>01000naa a22002652 4500</leader><controlfield tag="001">OLC2106607024</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20230403073213.0</controlfield><controlfield tag="007">tu</controlfield><controlfield tag="008">230403s2000 xx ||||| 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.1007/s004490000214</subfield><subfield code="2">doi</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)OLC2106607024</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-He213)s004490000214-p</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">570</subfield><subfield code="a">690</subfield><subfield code="a">540</subfield><subfield code="q">VZ</subfield></datafield><datafield tag="084" ind1=" " ind2=" "><subfield code="a">12</subfield><subfield code="2">ssgn</subfield></datafield><datafield tag="100" ind1="1" ind2=" "><subfield code="a">Banat, F. A.</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions via membrane distillation</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2000</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="500" ind1=" " ind2=" "><subfield code="a">© Springer-Verlag Berlin Heidelberg 2000</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Abstract The simultaneous recovery of dilute acetone–butanol–ethanol (ABE) solvents from aqueous solutions by air gap membrane distillation was theoretically assessed. A previously developed and validated Stefan–Maxwell based mathematical model was used for this purpose. It was found that membrane distillation could successfully be used for the recovery of these solvents. Interestingly it was found that butanol could be separated with the highest selectivity and flux though it has the highest boiling point. The effect of operating conditions such as feed and cooling surface temperatures, air gap width, and individual component concentration on the flux and selectivity of these solvents was examined and discussed in this paper.</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Aqueous Solution</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Acetone</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Surface Temperature</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Boiling</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Butanol</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Al-Shannag, M.</subfield><subfield code="4">aut</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">Enthalten in</subfield><subfield code="t">Bioprocess engineering</subfield><subfield code="d">Springer-Verlag, 1986</subfield><subfield code="g">23(2000), 6 vom: Dez., Seite 643-649</subfield><subfield code="w">(DE-627)129208922</subfield><subfield code="w">(DE-600)55154-5</subfield><subfield code="w">(DE-576)01445761X</subfield><subfield code="x">0178-515X</subfield><subfield code="7">nnns</subfield></datafield><datafield tag="773" ind1="1" ind2="8"><subfield code="g">volume:23</subfield><subfield code="g">year:2000</subfield><subfield code="g">number:6</subfield><subfield code="g">month:12</subfield><subfield code="g">pages:643-649</subfield></datafield><datafield tag="856" ind1="4" ind2="1"><subfield code="u">https://doi.org/10.1007/s004490000214</subfield><subfield code="z">lizenzpflichtig</subfield><subfield code="3">Volltext</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-ARC</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">GBV_ILN_11</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_23</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_32</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_40</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_65</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_2006</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_2018</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4046</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4277</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4307</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4310</subfield></datafield><datafield tag="912" ind1=" " ind2=" "><subfield code="a">GBV_ILN_4328</subfield></datafield><datafield tag="951" ind1=" " ind2=" "><subfield code="a">AR</subfield></datafield><datafield tag="952" ind1=" " ind2=" "><subfield code="d">23</subfield><subfield code="j">2000</subfield><subfield code="e">6</subfield><subfield code="c">12</subfield><subfield code="h">643-649</subfield></datafield></record></collection>
|
| score |
7.400174 |