Kinetic Study of Oxidative Dehydrogenation of Ethane over MoVTeNb Mixed-Oxide Catalyst
A MoVTeNb multimetallic mixed oxide was studied for the oxidative dehydrogenation of ethane, a promising alternative for catalytic ethylene production. Lab-scale steady-state experimental reaction data were obtained according to a 3k experimental design to investigate the simultaneous effect of temp...
Gespeichert in:
Veröffentlicht in: | Industrial & engineering chemistry research 2014-02, Vol.53 (5), p.1775-1786 |
---|---|
Hauptverfasser: | , , , , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
container_end_page | 1786 |
---|---|
container_issue | 5 |
container_start_page | 1775 |
container_title | Industrial & engineering chemistry research |
container_volume | 53 |
creator | Valente, Jaime S Quintana-Solórzano, R Armendáriz-Herrera, H Barragán-Rodríguez, G López-Nieto, J. M |
description | A MoVTeNb multimetallic mixed oxide was studied for the oxidative dehydrogenation of ethane, a promising alternative for catalytic ethylene production. Lab-scale steady-state experimental reaction data were obtained according to a 3k experimental design to investigate the simultaneous effect of temperature (400–480 °C) and space–time [23–70 gcat h (mol of ethane)−1]. A fixed-bed reactor at atmospheric pressure was employed, feeding a mixture of ethane, oxygen, and nitrogen. Ethane conversion varied from 17 to 85%, whereas selectivity for ethylene and CO x varied from 94 to 76% and from 4.0 to 24%, respectively. These types of analyses are useful for determining the optimum reaction conditions to enhance the catalytic performance of the mixed oxides presented herein. |
doi_str_mv | 10.1021/ie402447h |
format | Article |
fullrecord | <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_1692375117</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>1692375117</sourcerecordid><originalsourceid>FETCH-LOGICAL-a364t-c069a58cba7c226eb714028abb332b770663ada4c91fe49e6043f0855ab2b03a3</originalsourceid><addsrcrecordid>eNptkEtPwzAQhC0EEqVw4B_4ggSHgJ9JekSlPERLD5ReI9vZUFdpDLZTNf-eVEWcOK1G--1odhC6pOSWEkbvLAjChMhWR2hAJSOJJEIeowHJ8zyReS5P0VkIa0KIlEIM0PLVNhCtwe-xLTvsKjzf2VJFuwX8AKuu9O4Tml67Zr-cxJVqALsteDxzywW8aTyzOyiT_RngsYqq7kI8RyeVqgNc_M4h-nicLMbPyXT-9DK-nyaKpyImhqQjJXOjVWYYS0FntI-fK605ZzrLSJpyVSphRrQCMYKUCF6RXEqlmSZc8SG6Pvh-effdQojFxgYDdd2ndG0oaDpiPJOUZj16c0CNdyF4qIovbzfKdwUlxb674q-7nr06sMqEYu1a3_RP_MP9ALvMbNI</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>1692375117</pqid></control><display><type>article</type><title>Kinetic Study of Oxidative Dehydrogenation of Ethane over MoVTeNb Mixed-Oxide Catalyst</title><source>American Chemical Society</source><creator>Valente, Jaime S ; Quintana-Solórzano, R ; Armendáriz-Herrera, H ; Barragán-Rodríguez, G ; López-Nieto, J. M</creator><creatorcontrib>Valente, Jaime S ; Quintana-Solórzano, R ; Armendáriz-Herrera, H ; Barragán-Rodríguez, G ; López-Nieto, J. M</creatorcontrib><description>A MoVTeNb multimetallic mixed oxide was studied for the oxidative dehydrogenation of ethane, a promising alternative for catalytic ethylene production. Lab-scale steady-state experimental reaction data were obtained according to a 3k experimental design to investigate the simultaneous effect of temperature (400–480 °C) and space–time [23–70 gcat h (mol of ethane)−1]. A fixed-bed reactor at atmospheric pressure was employed, feeding a mixture of ethane, oxygen, and nitrogen. Ethane conversion varied from 17 to 85%, whereas selectivity for ethylene and CO x varied from 94 to 76% and from 4.0 to 24%, respectively. These types of analyses are useful for determining the optimum reaction conditions to enhance the catalytic performance of the mixed oxides presented herein.</description><identifier>ISSN: 0888-5885</identifier><identifier>EISSN: 1520-5045</identifier><identifier>DOI: 10.1021/ie402447h</identifier><language>eng</language><publisher>American Chemical Society</publisher><subject>Catalysis ; Catalysts ; Conversion ; Dehydrogenation ; Ethane ; Ethylene ; Feeding ; Mixed oxides</subject><ispartof>Industrial & engineering chemistry research, 2014-02, Vol.53 (5), p.1775-1786</ispartof><rights>Copyright © 2013 American Chemical Society</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-a364t-c069a58cba7c226eb714028abb332b770663ada4c91fe49e6043f0855ab2b03a3</citedby><cites>FETCH-LOGICAL-a364t-c069a58cba7c226eb714028abb332b770663ada4c91fe49e6043f0855ab2b03a3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://pubs.acs.org/doi/pdf/10.1021/ie402447h$$EPDF$$P50$$Gacs$$H</linktopdf><linktohtml>$$Uhttps://pubs.acs.org/doi/10.1021/ie402447h$$EHTML$$P50$$Gacs$$H</linktohtml><link.rule.ids>314,776,780,2752,27053,27901,27902,56713,56763</link.rule.ids></links><search><creatorcontrib>Valente, Jaime S</creatorcontrib><creatorcontrib>Quintana-Solórzano, R</creatorcontrib><creatorcontrib>Armendáriz-Herrera, H</creatorcontrib><creatorcontrib>Barragán-Rodríguez, G</creatorcontrib><creatorcontrib>López-Nieto, J. M</creatorcontrib><title>Kinetic Study of Oxidative Dehydrogenation of Ethane over MoVTeNb Mixed-Oxide Catalyst</title><title>Industrial & engineering chemistry research</title><addtitle>Ind. Eng. Chem. Res</addtitle><description>A MoVTeNb multimetallic mixed oxide was studied for the oxidative dehydrogenation of ethane, a promising alternative for catalytic ethylene production. Lab-scale steady-state experimental reaction data were obtained according to a 3k experimental design to investigate the simultaneous effect of temperature (400–480 °C) and space–time [23–70 gcat h (mol of ethane)−1]. A fixed-bed reactor at atmospheric pressure was employed, feeding a mixture of ethane, oxygen, and nitrogen. Ethane conversion varied from 17 to 85%, whereas selectivity for ethylene and CO x varied from 94 to 76% and from 4.0 to 24%, respectively. These types of analyses are useful for determining the optimum reaction conditions to enhance the catalytic performance of the mixed oxides presented herein.</description><subject>Catalysis</subject><subject>Catalysts</subject><subject>Conversion</subject><subject>Dehydrogenation</subject><subject>Ethane</subject><subject>Ethylene</subject><subject>Feeding</subject><subject>Mixed oxides</subject><issn>0888-5885</issn><issn>1520-5045</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2014</creationdate><recordtype>article</recordtype><recordid>eNptkEtPwzAQhC0EEqVw4B_4ggSHgJ9JekSlPERLD5ReI9vZUFdpDLZTNf-eVEWcOK1G--1odhC6pOSWEkbvLAjChMhWR2hAJSOJJEIeowHJ8zyReS5P0VkIa0KIlEIM0PLVNhCtwe-xLTvsKjzf2VJFuwX8AKuu9O4Tml67Zr-cxJVqALsteDxzywW8aTyzOyiT_RngsYqq7kI8RyeVqgNc_M4h-nicLMbPyXT-9DK-nyaKpyImhqQjJXOjVWYYS0FntI-fK605ZzrLSJpyVSphRrQCMYKUCF6RXEqlmSZc8SG6Pvh-effdQojFxgYDdd2ndG0oaDpiPJOUZj16c0CNdyF4qIovbzfKdwUlxb674q-7nr06sMqEYu1a3_RP_MP9ALvMbNI</recordid><startdate>20140205</startdate><enddate>20140205</enddate><creator>Valente, Jaime S</creator><creator>Quintana-Solórzano, R</creator><creator>Armendáriz-Herrera, H</creator><creator>Barragán-Rodríguez, G</creator><creator>López-Nieto, J. M</creator><general>American Chemical Society</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>8BQ</scope><scope>8FD</scope><scope>JG9</scope></search><sort><creationdate>20140205</creationdate><title>Kinetic Study of Oxidative Dehydrogenation of Ethane over MoVTeNb Mixed-Oxide Catalyst</title><author>Valente, Jaime S ; Quintana-Solórzano, R ; Armendáriz-Herrera, H ; Barragán-Rodríguez, G ; López-Nieto, J. M</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a364t-c069a58cba7c226eb714028abb332b770663ada4c91fe49e6043f0855ab2b03a3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2014</creationdate><topic>Catalysis</topic><topic>Catalysts</topic><topic>Conversion</topic><topic>Dehydrogenation</topic><topic>Ethane</topic><topic>Ethylene</topic><topic>Feeding</topic><topic>Mixed oxides</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Valente, Jaime S</creatorcontrib><creatorcontrib>Quintana-Solórzano, R</creatorcontrib><creatorcontrib>Armendáriz-Herrera, H</creatorcontrib><creatorcontrib>Barragán-Rodríguez, G</creatorcontrib><creatorcontrib>López-Nieto, J. M</creatorcontrib><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><jtitle>Industrial & engineering chemistry research</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Valente, Jaime S</au><au>Quintana-Solórzano, R</au><au>Armendáriz-Herrera, H</au><au>Barragán-Rodríguez, G</au><au>López-Nieto, J. M</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Kinetic Study of Oxidative Dehydrogenation of Ethane over MoVTeNb Mixed-Oxide Catalyst</atitle><jtitle>Industrial & engineering chemistry research</jtitle><addtitle>Ind. Eng. Chem. Res</addtitle><date>2014-02-05</date><risdate>2014</risdate><volume>53</volume><issue>5</issue><spage>1775</spage><epage>1786</epage><pages>1775-1786</pages><issn>0888-5885</issn><eissn>1520-5045</eissn><abstract>A MoVTeNb multimetallic mixed oxide was studied for the oxidative dehydrogenation of ethane, a promising alternative for catalytic ethylene production. Lab-scale steady-state experimental reaction data were obtained according to a 3k experimental design to investigate the simultaneous effect of temperature (400–480 °C) and space–time [23–70 gcat h (mol of ethane)−1]. A fixed-bed reactor at atmospheric pressure was employed, feeding a mixture of ethane, oxygen, and nitrogen. Ethane conversion varied from 17 to 85%, whereas selectivity for ethylene and CO x varied from 94 to 76% and from 4.0 to 24%, respectively. These types of analyses are useful for determining the optimum reaction conditions to enhance the catalytic performance of the mixed oxides presented herein.</abstract><pub>American Chemical Society</pub><doi>10.1021/ie402447h</doi><tpages>12</tpages><oa>free_for_read</oa></addata></record> |
fulltext | fulltext |
identifier | ISSN: 0888-5885 |
ispartof | Industrial & engineering chemistry research, 2014-02, Vol.53 (5), p.1775-1786 |
issn | 0888-5885 1520-5045 |
language | eng |
recordid | cdi_proquest_miscellaneous_1692375117 |
source | American Chemical Society |
subjects | Catalysis Catalysts Conversion Dehydrogenation Ethane Ethylene Feeding Mixed oxides |
title | Kinetic Study of Oxidative Dehydrogenation of Ethane over MoVTeNb Mixed-Oxide Catalyst |
url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-02-08T02%3A20%3A24IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Kinetic%20Study%20of%20Oxidative%20Dehydrogenation%20of%20Ethane%20over%20MoVTeNb%20Mixed-Oxide%20Catalyst&rft.jtitle=Industrial%20&%20engineering%20chemistry%20research&rft.au=Valente,%20Jaime%20S&rft.date=2014-02-05&rft.volume=53&rft.issue=5&rft.spage=1775&rft.epage=1786&rft.pages=1775-1786&rft.issn=0888-5885&rft.eissn=1520-5045&rft_id=info:doi/10.1021/ie402447h&rft_dat=%3Cproquest_cross%3E1692375117%3C/proquest_cross%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=1692375117&rft_id=info:pmid/&rfr_iscdi=true |