Dehydrogenation of propane in a combined membrane reactor with hydrogen-permeable palladium module
Abstract The basic features of the propane dehydrogenation reaction in a combined membrane reactor with a hydrogen-permeable palladium module and chromia-alumina catalyst (9.0 wt % Cr) in the temperature range of 520–580°C have been studied. Under optimum conditions (T, 550°C; propane space velocity...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Didenko, L. P. [verfasserIn] |
|---|
| Format: |
Artikel |
|---|---|
| Sprache: |
Englisch |
| Erschienen: |
2013 |
|---|
| Schlagwörter: |
|---|
| Anmerkung: |
© Pleiades Publishing, Ltd. 2013 |
|---|
| Übergeordnetes Werk: |
Enthalten in: Petroleum chemistry - SP MAIK Nauka/Interperiodica, 1962, 53(2013), 1 vom: Jan., Seite 27-32 |
|---|---|
| Übergeordnetes Werk: |
volume:53 ; year:2013 ; number:1 ; month:01 ; pages:27-32 |
| Links: |
|---|
| DOI / URN: |
10.1134/S0965544113010039 |
|---|
| Katalog-ID: |
OLC2042197254 |
|---|
| LEADER | 01000caa a22002652 4500 | ||
|---|---|---|---|
| 001 | OLC2042197254 | ||
| 003 | DE-627 | ||
| 005 | 20230511155018.0 | ||
| 007 | tu | ||
| 008 | 200819s2013 xx ||||| 00| ||eng c | ||
| 024 | 7 | |a 10.1134/S0965544113010039 |2 doi | |
| 035 | |a (DE-627)OLC2042197254 | ||
| 035 | |a (DE-He213)S0965544113010039-p | ||
| 040 | |a DE-627 |b ger |c DE-627 |e rakwb | ||
| 041 | |a eng | ||
| 082 | 0 | 4 | |a 690 |q VZ |
| 100 | 1 | |a Didenko, L. P. |e verfasserin |4 aut | |
| 245 | 1 | 0 | |a Dehydrogenation of propane in a combined membrane reactor with hydrogen-permeable palladium module |
| 264 | 1 | |c 2013 | |
| 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 © Pleiades Publishing, Ltd. 2013 | ||
| 520 | |a Abstract The basic features of the propane dehydrogenation reaction in a combined membrane reactor with a hydrogen-permeable palladium module and chromia-alumina catalyst (9.0 wt % Cr) in the temperature range of 520–580°C have been studied. Under optimum conditions (T, 550°C; propane space velocity and a stripping gas flow rate of 600–900 $ h^{−1} $ and 100–250 $ cm^{3} $/min, respectively), the feedstock conversion to propylene increases by a factor of 1.6–2.0. It has been suggested that compliance between the rate of $ H^{2} $ formation and its withdrawal through the membrane is of considerable importance. | ||
| 650 | 4 | |a palladium membrane module | |
| 650 | 4 | |a propane | |
| 650 | 4 | |a catalytic dehydrogenation | |
| 700 | 1 | |a Savchenko, V. I. |4 aut | |
| 700 | 1 | |a Sementsova, L. A. |4 aut | |
| 700 | 1 | |a Chizhov, P. E. |4 aut | |
| 700 | 1 | |a Bykov, L. A. |4 aut | |
| 773 | 0 | 8 | |i Enthalten in |t Petroleum chemistry |d SP MAIK Nauka/Interperiodica, 1962 |g 53(2013), 1 vom: Jan., Seite 27-32 |w (DE-627)129598399 |w (DE-600)241025-4 |w (DE-576)015091651 |x 0965-5441 |7 nnns |
| 773 | 1 | 8 | |g volume:53 |g year:2013 |g number:1 |g month:01 |g pages:27-32 |
| 856 | 4 | 1 | |u https://doi.org/10.1134/S0965544113010039 |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-PHA | ||
| 912 | |a SSG-OLC-DE-84 | ||
| 912 | |a GBV_ILN_70 | ||
| 951 | |a AR | ||
| 952 | |d 53 |j 2013 |e 1 |c 01 |h 27-32 | ||
| author_variant |
l p d lp lpd v i s vi vis l a s la las p e c pe pec l a b la lab |
|---|---|
| matchkey_str |
article:09655441:2013----::eyrgntoopoaencmiemmrnratrihyrgn |
| hierarchy_sort_str |
2013 |
| publishDate |
2013 |
| allfields |
10.1134/S0965544113010039 doi (DE-627)OLC2042197254 (DE-He213)S0965544113010039-p DE-627 ger DE-627 rakwb eng 690 VZ Didenko, L. P. verfasserin aut Dehydrogenation of propane in a combined membrane reactor with hydrogen-permeable palladium module 2013 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2013 Abstract The basic features of the propane dehydrogenation reaction in a combined membrane reactor with a hydrogen-permeable palladium module and chromia-alumina catalyst (9.0 wt % Cr) in the temperature range of 520–580°C have been studied. Under optimum conditions (T, 550°C; propane space velocity and a stripping gas flow rate of 600–900 $ h^{−1} $ and 100–250 $ cm^{3} $/min, respectively), the feedstock conversion to propylene increases by a factor of 1.6–2.0. It has been suggested that compliance between the rate of $ H^{2} $ formation and its withdrawal through the membrane is of considerable importance. palladium membrane module propane catalytic dehydrogenation Savchenko, V. I. aut Sementsova, L. A. aut Chizhov, P. E. aut Bykov, L. A. aut Enthalten in Petroleum chemistry SP MAIK Nauka/Interperiodica, 1962 53(2013), 1 vom: Jan., Seite 27-32 (DE-627)129598399 (DE-600)241025-4 (DE-576)015091651 0965-5441 nnns volume:53 year:2013 number:1 month:01 pages:27-32 https://doi.org/10.1134/S0965544113010039 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 53 2013 1 01 27-32 |
| spelling |
10.1134/S0965544113010039 doi (DE-627)OLC2042197254 (DE-He213)S0965544113010039-p DE-627 ger DE-627 rakwb eng 690 VZ Didenko, L. P. verfasserin aut Dehydrogenation of propane in a combined membrane reactor with hydrogen-permeable palladium module 2013 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2013 Abstract The basic features of the propane dehydrogenation reaction in a combined membrane reactor with a hydrogen-permeable palladium module and chromia-alumina catalyst (9.0 wt % Cr) in the temperature range of 520–580°C have been studied. Under optimum conditions (T, 550°C; propane space velocity and a stripping gas flow rate of 600–900 $ h^{−1} $ and 100–250 $ cm^{3} $/min, respectively), the feedstock conversion to propylene increases by a factor of 1.6–2.0. It has been suggested that compliance between the rate of $ H^{2} $ formation and its withdrawal through the membrane is of considerable importance. palladium membrane module propane catalytic dehydrogenation Savchenko, V. I. aut Sementsova, L. A. aut Chizhov, P. E. aut Bykov, L. A. aut Enthalten in Petroleum chemistry SP MAIK Nauka/Interperiodica, 1962 53(2013), 1 vom: Jan., Seite 27-32 (DE-627)129598399 (DE-600)241025-4 (DE-576)015091651 0965-5441 nnns volume:53 year:2013 number:1 month:01 pages:27-32 https://doi.org/10.1134/S0965544113010039 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 53 2013 1 01 27-32 |
| allfields_unstemmed |
10.1134/S0965544113010039 doi (DE-627)OLC2042197254 (DE-He213)S0965544113010039-p DE-627 ger DE-627 rakwb eng 690 VZ Didenko, L. P. verfasserin aut Dehydrogenation of propane in a combined membrane reactor with hydrogen-permeable palladium module 2013 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2013 Abstract The basic features of the propane dehydrogenation reaction in a combined membrane reactor with a hydrogen-permeable palladium module and chromia-alumina catalyst (9.0 wt % Cr) in the temperature range of 520–580°C have been studied. Under optimum conditions (T, 550°C; propane space velocity and a stripping gas flow rate of 600–900 $ h^{−1} $ and 100–250 $ cm^{3} $/min, respectively), the feedstock conversion to propylene increases by a factor of 1.6–2.0. It has been suggested that compliance between the rate of $ H^{2} $ formation and its withdrawal through the membrane is of considerable importance. palladium membrane module propane catalytic dehydrogenation Savchenko, V. I. aut Sementsova, L. A. aut Chizhov, P. E. aut Bykov, L. A. aut Enthalten in Petroleum chemistry SP MAIK Nauka/Interperiodica, 1962 53(2013), 1 vom: Jan., Seite 27-32 (DE-627)129598399 (DE-600)241025-4 (DE-576)015091651 0965-5441 nnns volume:53 year:2013 number:1 month:01 pages:27-32 https://doi.org/10.1134/S0965544113010039 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 53 2013 1 01 27-32 |
| allfieldsGer |
10.1134/S0965544113010039 doi (DE-627)OLC2042197254 (DE-He213)S0965544113010039-p DE-627 ger DE-627 rakwb eng 690 VZ Didenko, L. P. verfasserin aut Dehydrogenation of propane in a combined membrane reactor with hydrogen-permeable palladium module 2013 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2013 Abstract The basic features of the propane dehydrogenation reaction in a combined membrane reactor with a hydrogen-permeable palladium module and chromia-alumina catalyst (9.0 wt % Cr) in the temperature range of 520–580°C have been studied. Under optimum conditions (T, 550°C; propane space velocity and a stripping gas flow rate of 600–900 $ h^{−1} $ and 100–250 $ cm^{3} $/min, respectively), the feedstock conversion to propylene increases by a factor of 1.6–2.0. It has been suggested that compliance between the rate of $ H^{2} $ formation and its withdrawal through the membrane is of considerable importance. palladium membrane module propane catalytic dehydrogenation Savchenko, V. I. aut Sementsova, L. A. aut Chizhov, P. E. aut Bykov, L. A. aut Enthalten in Petroleum chemistry SP MAIK Nauka/Interperiodica, 1962 53(2013), 1 vom: Jan., Seite 27-32 (DE-627)129598399 (DE-600)241025-4 (DE-576)015091651 0965-5441 nnns volume:53 year:2013 number:1 month:01 pages:27-32 https://doi.org/10.1134/S0965544113010039 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 53 2013 1 01 27-32 |
| allfieldsSound |
10.1134/S0965544113010039 doi (DE-627)OLC2042197254 (DE-He213)S0965544113010039-p DE-627 ger DE-627 rakwb eng 690 VZ Didenko, L. P. verfasserin aut Dehydrogenation of propane in a combined membrane reactor with hydrogen-permeable palladium module 2013 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © Pleiades Publishing, Ltd. 2013 Abstract The basic features of the propane dehydrogenation reaction in a combined membrane reactor with a hydrogen-permeable palladium module and chromia-alumina catalyst (9.0 wt % Cr) in the temperature range of 520–580°C have been studied. Under optimum conditions (T, 550°C; propane space velocity and a stripping gas flow rate of 600–900 $ h^{−1} $ and 100–250 $ cm^{3} $/min, respectively), the feedstock conversion to propylene increases by a factor of 1.6–2.0. It has been suggested that compliance between the rate of $ H^{2} $ formation and its withdrawal through the membrane is of considerable importance. palladium membrane module propane catalytic dehydrogenation Savchenko, V. I. aut Sementsova, L. A. aut Chizhov, P. E. aut Bykov, L. A. aut Enthalten in Petroleum chemistry SP MAIK Nauka/Interperiodica, 1962 53(2013), 1 vom: Jan., Seite 27-32 (DE-627)129598399 (DE-600)241025-4 (DE-576)015091651 0965-5441 nnns volume:53 year:2013 number:1 month:01 pages:27-32 https://doi.org/10.1134/S0965544113010039 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 53 2013 1 01 27-32 |
| language |
English |
| source |
Enthalten in Petroleum chemistry 53(2013), 1 vom: Jan., Seite 27-32 volume:53 year:2013 number:1 month:01 pages:27-32 |
| sourceStr |
Enthalten in Petroleum chemistry 53(2013), 1 vom: Jan., Seite 27-32 volume:53 year:2013 number:1 month:01 pages:27-32 |
| format_phy_str_mv |
Article |
| institution |
findex.gbv.de |
| topic_facet |
palladium membrane module propane catalytic dehydrogenation |
| dewey-raw |
690 |
| isfreeaccess_bool |
false |
| container_title |
Petroleum chemistry |
| authorswithroles_txt_mv |
Didenko, L. P. @@aut@@ Savchenko, V. I. @@aut@@ Sementsova, L. A. @@aut@@ Chizhov, P. E. @@aut@@ Bykov, L. A. @@aut@@ |
| publishDateDaySort_date |
2013-01-01T00:00:00Z |
| hierarchy_top_id |
129598399 |
| dewey-sort |
3690 |
| id |
OLC2042197254 |
| language_de |
englisch |
| fullrecord |
<?xml version="1.0" encoding="UTF-8"?><collection xmlns="http://www.loc.gov/MARC21/slim"><record><leader>01000caa a22002652 4500</leader><controlfield tag="001">OLC2042197254</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20230511155018.0</controlfield><controlfield tag="007">tu</controlfield><controlfield tag="008">200819s2013 xx ||||| 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.1134/S0965544113010039</subfield><subfield code="2">doi</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)OLC2042197254</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-He213)S0965544113010039-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">690</subfield><subfield code="q">VZ</subfield></datafield><datafield tag="100" ind1="1" ind2=" "><subfield code="a">Didenko, L. P.</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Dehydrogenation of propane in a combined membrane reactor with hydrogen-permeable palladium module</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2013</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">© Pleiades Publishing, Ltd. 2013</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Abstract The basic features of the propane dehydrogenation reaction in a combined membrane reactor with a hydrogen-permeable palladium module and chromia-alumina catalyst (9.0 wt % Cr) in the temperature range of 520–580°C have been studied. Under optimum conditions (T, 550°C; propane space velocity and a stripping gas flow rate of 600–900 $ h^{−1} $ and 100–250 $ cm^{3} $/min, respectively), the feedstock conversion to propylene increases by a factor of 1.6–2.0. It has been suggested that compliance between the rate of $ H^{2} $ formation and its withdrawal through the membrane is of considerable importance.</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">palladium membrane module</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">propane</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">catalytic dehydrogenation</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Savchenko, V. I.</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Sementsova, L. A.</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Chizhov, P. E.</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Bykov, L. A.</subfield><subfield code="4">aut</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">Enthalten in</subfield><subfield code="t">Petroleum chemistry</subfield><subfield code="d">SP MAIK Nauka/Interperiodica, 1962</subfield><subfield code="g">53(2013), 1 vom: Jan., Seite 27-32</subfield><subfield code="w">(DE-627)129598399</subfield><subfield code="w">(DE-600)241025-4</subfield><subfield code="w">(DE-576)015091651</subfield><subfield code="x">0965-5441</subfield><subfield code="7">nnns</subfield></datafield><datafield tag="773" ind1="1" ind2="8"><subfield code="g">volume:53</subfield><subfield code="g">year:2013</subfield><subfield code="g">number:1</subfield><subfield code="g">month:01</subfield><subfield code="g">pages:27-32</subfield></datafield><datafield tag="856" ind1="4" ind2="1"><subfield code="u">https://doi.org/10.1134/S0965544113010039</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-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">53</subfield><subfield code="j">2013</subfield><subfield code="e">1</subfield><subfield code="c">01</subfield><subfield code="h">27-32</subfield></datafield></record></collection>
|
| author |
Didenko, L. P. |
| spellingShingle |
Didenko, L. P. ddc 690 misc palladium membrane module misc propane misc catalytic dehydrogenation Dehydrogenation of propane in a combined membrane reactor with hydrogen-permeable palladium module |
| authorStr |
Didenko, L. P. |
| ppnlink_with_tag_str_mv |
@@773@@(DE-627)129598399 |
| format |
Article |
| dewey-ones |
690 - Buildings |
| delete_txt_mv |
keep |
| author_role |
aut aut aut aut aut |
| collection |
OLC |
| remote_str |
false |
| illustrated |
Not Illustrated |
| issn |
0965-5441 |
| topic_title |
690 VZ Dehydrogenation of propane in a combined membrane reactor with hydrogen-permeable palladium module palladium membrane module propane catalytic dehydrogenation |
| topic |
ddc 690 misc palladium membrane module misc propane misc catalytic dehydrogenation |
| topic_unstemmed |
ddc 690 misc palladium membrane module misc propane misc catalytic dehydrogenation |
| topic_browse |
ddc 690 misc palladium membrane module misc propane misc catalytic dehydrogenation |
| format_facet |
Aufsätze Gedruckte Aufsätze |
| format_main_str_mv |
Text Zeitschrift/Artikel |
| carriertype_str_mv |
nc |
| hierarchy_parent_title |
Petroleum chemistry |
| hierarchy_parent_id |
129598399 |
| dewey-tens |
690 - Building & construction |
| hierarchy_top_title |
Petroleum chemistry |
| isfreeaccess_txt |
false |
| familylinks_str_mv |
(DE-627)129598399 (DE-600)241025-4 (DE-576)015091651 |
| title |
Dehydrogenation of propane in a combined membrane reactor with hydrogen-permeable palladium module |
| ctrlnum |
(DE-627)OLC2042197254 (DE-He213)S0965544113010039-p |
| title_full |
Dehydrogenation of propane in a combined membrane reactor with hydrogen-permeable palladium module |
| author_sort |
Didenko, L. P. |
| journal |
Petroleum chemistry |
| journalStr |
Petroleum chemistry |
| lang_code |
eng |
| isOA_bool |
false |
| dewey-hundreds |
600 - Technology |
| recordtype |
marc |
| publishDateSort |
2013 |
| contenttype_str_mv |
txt |
| container_start_page |
27 |
| author_browse |
Didenko, L. P. Savchenko, V. I. Sementsova, L. A. Chizhov, P. E. Bykov, L. A. |
| container_volume |
53 |
| class |
690 VZ |
| format_se |
Aufsätze |
| author-letter |
Didenko, L. P. |
| doi_str_mv |
10.1134/S0965544113010039 |
| dewey-full |
690 |
| title_sort |
dehydrogenation of propane in a combined membrane reactor with hydrogen-permeable palladium module |
| title_auth |
Dehydrogenation of propane in a combined membrane reactor with hydrogen-permeable palladium module |
| abstract |
Abstract The basic features of the propane dehydrogenation reaction in a combined membrane reactor with a hydrogen-permeable palladium module and chromia-alumina catalyst (9.0 wt % Cr) in the temperature range of 520–580°C have been studied. Under optimum conditions (T, 550°C; propane space velocity and a stripping gas flow rate of 600–900 $ h^{−1} $ and 100–250 $ cm^{3} $/min, respectively), the feedstock conversion to propylene increases by a factor of 1.6–2.0. It has been suggested that compliance between the rate of $ H^{2} $ formation and its withdrawal through the membrane is of considerable importance. © Pleiades Publishing, Ltd. 2013 |
| abstractGer |
Abstract The basic features of the propane dehydrogenation reaction in a combined membrane reactor with a hydrogen-permeable palladium module and chromia-alumina catalyst (9.0 wt % Cr) in the temperature range of 520–580°C have been studied. Under optimum conditions (T, 550°C; propane space velocity and a stripping gas flow rate of 600–900 $ h^{−1} $ and 100–250 $ cm^{3} $/min, respectively), the feedstock conversion to propylene increases by a factor of 1.6–2.0. It has been suggested that compliance between the rate of $ H^{2} $ formation and its withdrawal through the membrane is of considerable importance. © Pleiades Publishing, Ltd. 2013 |
| abstract_unstemmed |
Abstract The basic features of the propane dehydrogenation reaction in a combined membrane reactor with a hydrogen-permeable palladium module and chromia-alumina catalyst (9.0 wt % Cr) in the temperature range of 520–580°C have been studied. Under optimum conditions (T, 550°C; propane space velocity and a stripping gas flow rate of 600–900 $ h^{−1} $ and 100–250 $ cm^{3} $/min, respectively), the feedstock conversion to propylene increases by a factor of 1.6–2.0. It has been suggested that compliance between the rate of $ H^{2} $ formation and its withdrawal through the membrane is of considerable importance. © Pleiades Publishing, Ltd. 2013 |
| collection_details |
GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-UMW SSG-OLC-ARC SSG-OLC-TEC SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 |
| container_issue |
1 |
| title_short |
Dehydrogenation of propane in a combined membrane reactor with hydrogen-permeable palladium module |
| url |
https://doi.org/10.1134/S0965544113010039 |
| remote_bool |
false |
| author2 |
Savchenko, V. I. Sementsova, L. A. Chizhov, P. E. Bykov, L. A. |
| author2Str |
Savchenko, V. I. Sementsova, L. A. Chizhov, P. E. Bykov, L. A. |
| ppnlink |
129598399 |
| mediatype_str_mv |
n |
| isOA_txt |
false |
| hochschulschrift_bool |
false |
| doi_str |
10.1134/S0965544113010039 |
| up_date |
2024-07-03T14:11:29.791Z |
| _version_ |
1803567381652439040 |
| fullrecord_marcxml |
<?xml version="1.0" encoding="UTF-8"?><collection xmlns="http://www.loc.gov/MARC21/slim"><record><leader>01000caa a22002652 4500</leader><controlfield tag="001">OLC2042197254</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20230511155018.0</controlfield><controlfield tag="007">tu</controlfield><controlfield tag="008">200819s2013 xx ||||| 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.1134/S0965544113010039</subfield><subfield code="2">doi</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)OLC2042197254</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-He213)S0965544113010039-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">690</subfield><subfield code="q">VZ</subfield></datafield><datafield tag="100" ind1="1" ind2=" "><subfield code="a">Didenko, L. P.</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Dehydrogenation of propane in a combined membrane reactor with hydrogen-permeable palladium module</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2013</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">© Pleiades Publishing, Ltd. 2013</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Abstract The basic features of the propane dehydrogenation reaction in a combined membrane reactor with a hydrogen-permeable palladium module and chromia-alumina catalyst (9.0 wt % Cr) in the temperature range of 520–580°C have been studied. Under optimum conditions (T, 550°C; propane space velocity and a stripping gas flow rate of 600–900 $ h^{−1} $ and 100–250 $ cm^{3} $/min, respectively), the feedstock conversion to propylene increases by a factor of 1.6–2.0. It has been suggested that compliance between the rate of $ H^{2} $ formation and its withdrawal through the membrane is of considerable importance.</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">palladium membrane module</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">propane</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">catalytic dehydrogenation</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Savchenko, V. I.</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Sementsova, L. A.</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Chizhov, P. E.</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Bykov, L. A.</subfield><subfield code="4">aut</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">Enthalten in</subfield><subfield code="t">Petroleum chemistry</subfield><subfield code="d">SP MAIK Nauka/Interperiodica, 1962</subfield><subfield code="g">53(2013), 1 vom: Jan., Seite 27-32</subfield><subfield code="w">(DE-627)129598399</subfield><subfield code="w">(DE-600)241025-4</subfield><subfield code="w">(DE-576)015091651</subfield><subfield code="x">0965-5441</subfield><subfield code="7">nnns</subfield></datafield><datafield tag="773" ind1="1" ind2="8"><subfield code="g">volume:53</subfield><subfield code="g">year:2013</subfield><subfield code="g">number:1</subfield><subfield code="g">month:01</subfield><subfield code="g">pages:27-32</subfield></datafield><datafield tag="856" ind1="4" ind2="1"><subfield code="u">https://doi.org/10.1134/S0965544113010039</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-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">53</subfield><subfield code="j">2013</subfield><subfield code="e">1</subfield><subfield code="c">01</subfield><subfield code="h">27-32</subfield></datafield></record></collection>
|
| score |
7.402011 |