Oxidative conversion of ethane over VMoTeNb oxide catalyst
The oxidative conversion of ethane over a multicomponent oxide catalyst with the composition V 0.3 Mo 1 Te 0.23 Nb 0.12 was studied in the temperature range of 360–450°C. It was found that temperature did not affect the contribution from the parallel and consecutive paths of reaction product formati...
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| Veröffentlicht in: | Catalysis in industry 2016-04, Vol.8 (2), p.112-115 |
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| container_title | Catalysis in industry |
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| creator | Bondareva, V. M. Ishchenko, E. V. Shadrina, L. A. Sobolev, V. I. |
| description | The oxidative conversion of ethane over a multicomponent oxide catalyst with the composition V
0.3
Mo
1
Te
0.23
Nb
0.12
was studied in the temperature range of 360–450°C. It was found that temperature did not affect the contribution from the parallel and consecutive paths of reaction product formation. The obtained data could be useful in developing applications for the process, particularly in choosing the type and design of a reactor (tubular fixed bed, fluidized bed, and so on). |
| doi_str_mv | 10.1134/S2070050416020033 |
| format | Article |
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0.3
Mo
1
Te
0.23
Nb
0.12
was studied in the temperature range of 360–450°C. It was found that temperature did not affect the contribution from the parallel and consecutive paths of reaction product formation. The obtained data could be useful in developing applications for the process, particularly in choosing the type and design of a reactor (tubular fixed bed, fluidized bed, and so on).</description><identifier>ISSN: 2070-0504</identifier><identifier>EISSN: 2070-0555</identifier><identifier>DOI: 10.1134/S2070050416020033</identifier><language>eng</language><publisher>Moscow: Pleiades Publishing</publisher><subject>Catalysis ; Catalysis in Chemical and Petrochemical Industry ; Chemistry ; Chemistry and Materials Science</subject><ispartof>Catalysis in industry, 2016-04, Vol.8 (2), p.112-115</ispartof><rights>Pleiades Publishing, Ltd. 2016</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c325t-734049089c9cba3768503bfb463d909b79dd8a41096d8335962986ae3f06f1d3</citedby><cites>FETCH-LOGICAL-c325t-734049089c9cba3768503bfb463d909b79dd8a41096d8335962986ae3f06f1d3</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/S2070050416020033$$EPDF$$P50$$Gspringer$$H</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1134/S2070050416020033$$EHTML$$P50$$Gspringer$$H</linktohtml><link.rule.ids>314,780,784,27924,27925,41488,42557,51319</link.rule.ids></links><search><creatorcontrib>Bondareva, V. M.</creatorcontrib><creatorcontrib>Ishchenko, E. V.</creatorcontrib><creatorcontrib>Shadrina, L. A.</creatorcontrib><creatorcontrib>Sobolev, V. I.</creatorcontrib><title>Oxidative conversion of ethane over VMoTeNb oxide catalyst</title><title>Catalysis in industry</title><addtitle>Catal. Ind</addtitle><description>The oxidative conversion of ethane over a multicomponent oxide catalyst with the composition V
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Mo
1
Te
0.23
Nb
0.12
was studied in the temperature range of 360–450°C. It was found that temperature did not affect the contribution from the parallel and consecutive paths of reaction product formation. The obtained data could be useful in developing applications for the process, particularly in choosing the type and design of a reactor (tubular fixed bed, fluidized bed, and so on).</description><subject>Catalysis</subject><subject>Catalysis in Chemical and Petrochemical Industry</subject><subject>Chemistry</subject><subject>Chemistry and Materials Science</subject><issn>2070-0504</issn><issn>2070-0555</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2016</creationdate><recordtype>article</recordtype><recordid>eNp9j09LAzEQxYMoWGo_gLd8gdVJJskm3qT4D6o9WLwu2U2iW-pGkrXYb29KxYvgXGZ4_N7wHiHnDC4YQ3H5zKEGkCCYAg6AeEQme6kCKeXx7w3ilMxyXkMZboyp9YRcLb96Z8d-62kXh61PuY8DjYH68c0OnsYi0ZfHuPJPLY2FLZwd7WaXxzNyEuwm-9nPnpLV7c1qfl8tlncP8-tF1SGXY1WjAGFAm850rcVaaQnYhlYodAZMWxvntBUMjHIaURrFjVbWYwAVmMMpYYe3XYo5Jx-aj9S_27RrGDT7-s2f-sXDD55c2OHVp2YdP9NQUv5j-gZYkVo0</recordid><startdate>20160401</startdate><enddate>20160401</enddate><creator>Bondareva, V. M.</creator><creator>Ishchenko, E. V.</creator><creator>Shadrina, L. A.</creator><creator>Sobolev, V. I.</creator><general>Pleiades Publishing</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20160401</creationdate><title>Oxidative conversion of ethane over VMoTeNb oxide catalyst</title><author>Bondareva, V. M. ; Ishchenko, E. V. ; Shadrina, L. A. ; Sobolev, V. I.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c325t-734049089c9cba3768503bfb463d909b79dd8a41096d8335962986ae3f06f1d3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2016</creationdate><topic>Catalysis</topic><topic>Catalysis in Chemical and Petrochemical Industry</topic><topic>Chemistry</topic><topic>Chemistry and Materials Science</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Bondareva, V. M.</creatorcontrib><creatorcontrib>Ishchenko, E. V.</creatorcontrib><creatorcontrib>Shadrina, L. A.</creatorcontrib><creatorcontrib>Sobolev, V. I.</creatorcontrib><collection>CrossRef</collection><jtitle>Catalysis in industry</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Bondareva, V. M.</au><au>Ishchenko, E. V.</au><au>Shadrina, L. A.</au><au>Sobolev, V. I.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Oxidative conversion of ethane over VMoTeNb oxide catalyst</atitle><jtitle>Catalysis in industry</jtitle><stitle>Catal. Ind</stitle><date>2016-04-01</date><risdate>2016</risdate><volume>8</volume><issue>2</issue><spage>112</spage><epage>115</epage><pages>112-115</pages><issn>2070-0504</issn><eissn>2070-0555</eissn><abstract>The oxidative conversion of ethane over a multicomponent oxide catalyst with the composition V
0.3
Mo
1
Te
0.23
Nb
0.12
was studied in the temperature range of 360–450°C. It was found that temperature did not affect the contribution from the parallel and consecutive paths of reaction product formation. The obtained data could be useful in developing applications for the process, particularly in choosing the type and design of a reactor (tubular fixed bed, fluidized bed, and so on).</abstract><cop>Moscow</cop><pub>Pleiades Publishing</pub><doi>10.1134/S2070050416020033</doi><tpages>4</tpages></addata></record> |
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| ispartof | Catalysis in industry, 2016-04, Vol.8 (2), p.112-115 |
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| language | eng |
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| subjects | Catalysis Catalysis in Chemical and Petrochemical Industry Chemistry Chemistry and Materials Science |
| title | Oxidative conversion of ethane over VMoTeNb oxide catalyst |
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