Pd/Ga2O3–Al2O3 catalysts for the selective liquid-phase hydrogenation of acetylene to ethylene
The structure of Ga 2 O 3 –Al 2 O 3 supports and Pd/Ga 2 O 3 –Al 2 O 3 catalysts and the performance of these catalysts in liquid-phase acetylene hydrogenation have been investigated. The deposition of Ga(NO 3 ) 3 onto Al 2 O 3 by impregnation followed by calcination of the impregnated support at 60...
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Veröffentlicht in: | Kinetics and catalysis 2016-07, Vol.57 (4), p.490-496 |
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creator | Afonasenko, T. N. Smirnova, N. S. Temerev, V. L. Leont’eva, N. N. Gulyaeva, T. I. Tsyrul’nikov, P. G. |
description | The structure of Ga
2
O
3
–Al
2
O
3
supports and Pd/Ga
2
O
3
–Al
2
O
3
catalysts and the performance of these catalysts in liquid-phase acetylene hydrogenation have been investigated. The deposition of Ga(NO
3
)
3
onto Al
2
O
3
by impregnation followed by calcination of the impregnated support at 600°C yields γ-Ga
2
O
3
–Al
2
O
3
solid solutions containing up to 50 wt % Ga
2
O
3
. X-ray diffraction characterization of model palladium catalysts and their temperature-programmed reduction with hydrogen have demonstrated that, while palladium in Pd/Ga
2
O
3
is in the form of a Pd
2
Ga alloy, in the Pd/γ-Ga
2
O
3
–Al
2
O
3
catalyst there is no direct interaction between PdО and Ga
2
O
3
particles and palladium is in the monometallic state. The introduction of 10–20 wt % gallium oxide into Al
2
O
3
lowers the activity of the supported palladium catalyst relative to that of the initial Pd/Al
2
O
3
but increases the ethylene yield by enhancing the ethylene formation selectivity. |
doi_str_mv | 10.1134/S0023158416040017 |
format | Article |
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2
O
3
–Al
2
O
3
supports and Pd/Ga
2
O
3
–Al
2
O
3
catalysts and the performance of these catalysts in liquid-phase acetylene hydrogenation have been investigated. The deposition of Ga(NO
3
)
3
onto Al
2
O
3
by impregnation followed by calcination of the impregnated support at 600°C yields γ-Ga
2
O
3
–Al
2
O
3
solid solutions containing up to 50 wt % Ga
2
O
3
. X-ray diffraction characterization of model palladium catalysts and their temperature-programmed reduction with hydrogen have demonstrated that, while palladium in Pd/Ga
2
O
3
is in the form of a Pd
2
Ga alloy, in the Pd/γ-Ga
2
O
3
–Al
2
O
3
catalyst there is no direct interaction between PdО and Ga
2
O
3
particles and palladium is in the monometallic state. The introduction of 10–20 wt % gallium oxide into Al
2
O
3
lowers the activity of the supported palladium catalyst relative to that of the initial Pd/Al
2
O
3
but increases the ethylene yield by enhancing the ethylene formation selectivity.</description><identifier>ISSN: 0023-1584</identifier><identifier>EISSN: 1608-3210</identifier><identifier>DOI: 10.1134/S0023158416040017</identifier><language>eng</language><publisher>Moscow: Pleiades Publishing</publisher><subject>Catalysis ; Chemistry ; Chemistry and Materials Science ; Physical Chemistry</subject><ispartof>Kinetics and catalysis, 2016-07, Vol.57 (4), p.490-496</ispartof><rights>Pleiades Publishing, Ltd. 2016</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c325t-b23154597d43fff923c5bbbb9c62cffe73666064e305e2389070a8cabd9979573</citedby><cites>FETCH-LOGICAL-c325t-b23154597d43fff923c5bbbb9c62cffe73666064e305e2389070a8cabd9979573</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://link.springer.com/content/pdf/10.1134/S0023158416040017$$EPDF$$P50$$Gspringer$$H</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1134/S0023158416040017$$EHTML$$P50$$Gspringer$$H</linktohtml><link.rule.ids>314,776,780,27901,27902,41464,42533,51294</link.rule.ids></links><search><creatorcontrib>Afonasenko, T. N.</creatorcontrib><creatorcontrib>Smirnova, N. S.</creatorcontrib><creatorcontrib>Temerev, V. L.</creatorcontrib><creatorcontrib>Leont’eva, N. N.</creatorcontrib><creatorcontrib>Gulyaeva, T. I.</creatorcontrib><creatorcontrib>Tsyrul’nikov, P. G.</creatorcontrib><title>Pd/Ga2O3–Al2O3 catalysts for the selective liquid-phase hydrogenation of acetylene to ethylene</title><title>Kinetics and catalysis</title><addtitle>Kinet Catal</addtitle><description>The structure of Ga
2
O
3
–Al
2
O
3
supports and Pd/Ga
2
O
3
–Al
2
O
3
catalysts and the performance of these catalysts in liquid-phase acetylene hydrogenation have been investigated. The deposition of Ga(NO
3
)
3
onto Al
2
O
3
by impregnation followed by calcination of the impregnated support at 600°C yields γ-Ga
2
O
3
–Al
2
O
3
solid solutions containing up to 50 wt % Ga
2
O
3
. X-ray diffraction characterization of model palladium catalysts and their temperature-programmed reduction with hydrogen have demonstrated that, while palladium in Pd/Ga
2
O
3
is in the form of a Pd
2
Ga alloy, in the Pd/γ-Ga
2
O
3
–Al
2
O
3
catalyst there is no direct interaction between PdО and Ga
2
O
3
particles and palladium is in the monometallic state. The introduction of 10–20 wt % gallium oxide into Al
2
O
3
lowers the activity of the supported palladium catalyst relative to that of the initial Pd/Al
2
O
3
but increases the ethylene yield by enhancing the ethylene formation selectivity.</description><subject>Catalysis</subject><subject>Chemistry</subject><subject>Chemistry and Materials Science</subject><subject>Physical Chemistry</subject><issn>0023-1584</issn><issn>1608-3210</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2016</creationdate><recordtype>article</recordtype><recordid>eNp9UEtOwzAUtBBIlMIB2PkCoc-ffLysKihIlUAC1sF1nptUIS62i5Qdd-CGnISEskPibWakmXkaDSGXDK4YE3L2CMAFSwvJMpAALD8ik4EWieAMjslklJNRPyVnIWwBQDKpJuTloZotNb8XXx-f83ZAanTUbR9ioNZ5GmukAVs0sXlH2jZv-6ZKdrUOSOu-8m6DnY6N66izVBuMfYsd0ugoxvqHn5MTq9uAF784Jc8310-L22R1v7xbzFeJETyNyXpsL1OVV1JYaxUXJl0Pp0zGjbWYiyzLIJMoIEUuCgU56MLodaVUrtJcTAk7_DXeheDRljvfvGrflwzKcaLyz0RDhh8yYfB2G_Tl1u19N9T8J_QNCcZo8Q</recordid><startdate>20160701</startdate><enddate>20160701</enddate><creator>Afonasenko, T. N.</creator><creator>Smirnova, N. S.</creator><creator>Temerev, V. L.</creator><creator>Leont’eva, N. N.</creator><creator>Gulyaeva, T. I.</creator><creator>Tsyrul’nikov, P. G.</creator><general>Pleiades Publishing</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20160701</creationdate><title>Pd/Ga2O3–Al2O3 catalysts for the selective liquid-phase hydrogenation of acetylene to ethylene</title><author>Afonasenko, T. N. ; Smirnova, N. S. ; Temerev, V. L. ; Leont’eva, N. N. ; Gulyaeva, T. I. ; Tsyrul’nikov, P. G.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c325t-b23154597d43fff923c5bbbb9c62cffe73666064e305e2389070a8cabd9979573</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2016</creationdate><topic>Catalysis</topic><topic>Chemistry</topic><topic>Chemistry and Materials Science</topic><topic>Physical Chemistry</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Afonasenko, T. N.</creatorcontrib><creatorcontrib>Smirnova, N. S.</creatorcontrib><creatorcontrib>Temerev, V. L.</creatorcontrib><creatorcontrib>Leont’eva, N. N.</creatorcontrib><creatorcontrib>Gulyaeva, T. I.</creatorcontrib><creatorcontrib>Tsyrul’nikov, P. G.</creatorcontrib><collection>CrossRef</collection><jtitle>Kinetics and catalysis</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Afonasenko, T. N.</au><au>Smirnova, N. S.</au><au>Temerev, V. L.</au><au>Leont’eva, N. N.</au><au>Gulyaeva, T. I.</au><au>Tsyrul’nikov, P. G.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Pd/Ga2O3–Al2O3 catalysts for the selective liquid-phase hydrogenation of acetylene to ethylene</atitle><jtitle>Kinetics and catalysis</jtitle><stitle>Kinet Catal</stitle><date>2016-07-01</date><risdate>2016</risdate><volume>57</volume><issue>4</issue><spage>490</spage><epage>496</epage><pages>490-496</pages><issn>0023-1584</issn><eissn>1608-3210</eissn><abstract>The structure of Ga
2
O
3
–Al
2
O
3
supports and Pd/Ga
2
O
3
–Al
2
O
3
catalysts and the performance of these catalysts in liquid-phase acetylene hydrogenation have been investigated. The deposition of Ga(NO
3
)
3
onto Al
2
O
3
by impregnation followed by calcination of the impregnated support at 600°C yields γ-Ga
2
O
3
–Al
2
O
3
solid solutions containing up to 50 wt % Ga
2
O
3
. X-ray diffraction characterization of model palladium catalysts and their temperature-programmed reduction with hydrogen have demonstrated that, while palladium in Pd/Ga
2
O
3
is in the form of a Pd
2
Ga alloy, in the Pd/γ-Ga
2
O
3
–Al
2
O
3
catalyst there is no direct interaction between PdО and Ga
2
O
3
particles and palladium is in the monometallic state. The introduction of 10–20 wt % gallium oxide into Al
2
O
3
lowers the activity of the supported palladium catalyst relative to that of the initial Pd/Al
2
O
3
but increases the ethylene yield by enhancing the ethylene formation selectivity.</abstract><cop>Moscow</cop><pub>Pleiades Publishing</pub><doi>10.1134/S0023158416040017</doi><tpages>7</tpages></addata></record> |
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issn | 0023-1584 1608-3210 |
language | eng |
recordid | cdi_crossref_primary_10_1134_S0023158416040017 |
source | Springer Nature - Complete Springer Journals |
subjects | Catalysis Chemistry Chemistry and Materials Science Physical Chemistry |
title | Pd/Ga2O3–Al2O3 catalysts for the selective liquid-phase hydrogenation of acetylene to ethylene |
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