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Reduction and metathesis activity of MoO[sub 3]/Al[sub 2]O[sub 3] catalysts. II. The activation of MoO[sub 3]/Al[sub 2]O[sub 3] catalysts
MoO[sub 3]/Al[sub 2]O[sub 3] catalysts (0.5-13 wt% MoO[sub 3]) were activated for the metathesis of propene by thermal treatment in flowing inert gas and by reduction in H[sub 2] (reaction conditions: 473 K, 0.1 MPa). Temperatures between 900 and 1140 K were applied for the activation of the catalys...
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Published in: | Journal of catalysis 1992-05, Vol.135:1 |
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container_title | Journal of catalysis |
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creator | Gruenert, W. Feldhaus, R. Anders, K. Stakheev, A.Y. Shpiro, E.S. Minachev, K.M. |
description | MoO[sub 3]/Al[sub 2]O[sub 3] catalysts (0.5-13 wt% MoO[sub 3]) were activated for the metathesis of propene by thermal treatment in flowing inert gas and by reduction in H[sub 2] (reaction conditions: 473 K, 0.1 MPa). Temperatures between 900 and 1140 K were applied for the activation of the catalysts in inert atmosphere. The activity of the supported Mo (molecules/s Mo) increased with decreasing MoO[sub 3] content, which is opposite to the well-known trends for the reducibility of Mo(VI)/Al[sub 2]O[sub 3]. The kinetic reaction order of the propene metathesis was found to be 0.8 at 473 K. The apparent activation energy was 30-37 kJ/mole, with a slight decrease at increasing MoO[sub 3] content. The response of the activity to the extent of reduction was investigated at different reduction temperatures and MoO[sub 3] contents. From these observations and the results of the thermal activation study, it has been concluded that the active sites of metathesis can be formed from both Mo(VI) and Mo(IV) precursors. These precursors coexist on reduced surfaces, while the activity attained after thermal activation in inert gas is due exclusively to sites originating from mo(VI) species. Other Mo states (Mo(V), and Mo(II), and MO(0)) do not contribute to the metathesis activity. |
doi_str_mv | 10.1016/0021-9517(92)90286-Q |
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The activation of MoO[sub 3]/Al[sub 2]O[sub 3] catalysts</title><source>Backfile Package - Chemical Engineering (Legacy) [YCC]</source><creator>Gruenert, W. ; Feldhaus, R. ; Anders, K. ; Stakheev, A.Y. ; Shpiro, E.S. ; Minachev, K.M.</creator><creatorcontrib>Gruenert, W. ; Feldhaus, R. ; Anders, K. ; Stakheev, A.Y. ; Shpiro, E.S. ; Minachev, K.M.</creatorcontrib><description>MoO[sub 3]/Al[sub 2]O[sub 3] catalysts (0.5-13 wt% MoO[sub 3]) were activated for the metathesis of propene by thermal treatment in flowing inert gas and by reduction in H[sub 2] (reaction conditions: 473 K, 0.1 MPa). Temperatures between 900 and 1140 K were applied for the activation of the catalysts in inert atmosphere. The activity of the supported Mo (molecules/s Mo) increased with decreasing MoO[sub 3] content, which is opposite to the well-known trends for the reducibility of Mo(VI)/Al[sub 2]O[sub 3]. The kinetic reaction order of the propene metathesis was found to be 0.8 at 473 K. The apparent activation energy was 30-37 kJ/mole, with a slight decrease at increasing MoO[sub 3] content. The response of the activity to the extent of reduction was investigated at different reduction temperatures and MoO[sub 3] contents. From these observations and the results of the thermal activation study, it has been concluded that the active sites of metathesis can be formed from both Mo(VI) and Mo(IV) precursors. These precursors coexist on reduced surfaces, while the activity attained after thermal activation in inert gas is due exclusively to sites originating from mo(VI) species. Other Mo states (Mo(V), and Mo(II), and MO(0)) do not contribute to the metathesis activity.</description><identifier>ISSN: 0021-9517</identifier><identifier>EISSN: 1090-2694</identifier><identifier>DOI: 10.1016/0021-9517(92)90286-Q</identifier><language>eng</language><publisher>United States</publisher><subject>02 PETROLEUM ; 020400 - Petroleum- Processing ; 400201 - Chemical & Physicochemical Properties ; ACTIVATION ENERGY ; ALKENES ; ALUMINIUM COMPOUNDS ; ALUMINIUM OXIDES ; CATALYST SUPPORTS ; CATALYSTS ; CATALYTIC EFFECTS ; CHALCOGENIDES ; CHEMICAL ACTIVATION ; CHEMICAL REACTION KINETICS ; CHEMICAL REACTIONS ; ENERGY ; HEAT TREATMENTS ; HYDROCARBONS ; INORGANIC, ORGANIC, PHYSICAL AND ANALYTICAL CHEMISTRY ; ISOMERIZATION ; KINETICS ; MOLYBDENUM COMPOUNDS ; MOLYBDENUM OXIDES ; ORGANIC COMPOUNDS ; OXIDES ; OXYGEN COMPOUNDS ; PRECURSOR ; PROPYLENE ; REACTION KINETICS ; REDUCTION ; REFRACTORY METAL COMPOUNDS ; SURFACE PROPERTIES ; TEMPERATURE RANGE ; TEMPERATURE RANGE 0400-1000 K ; TEMPERATURE RANGE 1000-4000 K ; TRANSITION ELEMENT COMPOUNDS ; VALENCE</subject><ispartof>Journal of catalysis, 1992-05, Vol.135:1</ispartof><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>230,314,780,784,885,27924,27925</link.rule.ids><backlink>$$Uhttps://www.osti.gov/biblio/6975923$$D View this record in Osti.gov$$Hfree_for_read</backlink></links><search><creatorcontrib>Gruenert, W.</creatorcontrib><creatorcontrib>Feldhaus, R.</creatorcontrib><creatorcontrib>Anders, K.</creatorcontrib><creatorcontrib>Stakheev, A.Y.</creatorcontrib><creatorcontrib>Shpiro, E.S.</creatorcontrib><creatorcontrib>Minachev, K.M.</creatorcontrib><title>Reduction and metathesis activity of MoO[sub 3]/Al[sub 2]O[sub 3] catalysts. II. The activation of MoO[sub 3]/Al[sub 2]O[sub 3] catalysts</title><title>Journal of catalysis</title><description>MoO[sub 3]/Al[sub 2]O[sub 3] catalysts (0.5-13 wt% MoO[sub 3]) were activated for the metathesis of propene by thermal treatment in flowing inert gas and by reduction in H[sub 2] (reaction conditions: 473 K, 0.1 MPa). Temperatures between 900 and 1140 K were applied for the activation of the catalysts in inert atmosphere. The activity of the supported Mo (molecules/s Mo) increased with decreasing MoO[sub 3] content, which is opposite to the well-known trends for the reducibility of Mo(VI)/Al[sub 2]O[sub 3]. The kinetic reaction order of the propene metathesis was found to be 0.8 at 473 K. The apparent activation energy was 30-37 kJ/mole, with a slight decrease at increasing MoO[sub 3] content. The response of the activity to the extent of reduction was investigated at different reduction temperatures and MoO[sub 3] contents. From these observations and the results of the thermal activation study, it has been concluded that the active sites of metathesis can be formed from both Mo(VI) and Mo(IV) precursors. These precursors coexist on reduced surfaces, while the activity attained after thermal activation in inert gas is due exclusively to sites originating from mo(VI) species. Other Mo states (Mo(V), and Mo(II), and MO(0)) do not contribute to the metathesis activity.</description><subject>02 PETROLEUM</subject><subject>020400 - Petroleum- Processing</subject><subject>400201 - Chemical & Physicochemical Properties</subject><subject>ACTIVATION ENERGY</subject><subject>ALKENES</subject><subject>ALUMINIUM COMPOUNDS</subject><subject>ALUMINIUM OXIDES</subject><subject>CATALYST SUPPORTS</subject><subject>CATALYSTS</subject><subject>CATALYTIC EFFECTS</subject><subject>CHALCOGENIDES</subject><subject>CHEMICAL ACTIVATION</subject><subject>CHEMICAL REACTION KINETICS</subject><subject>CHEMICAL REACTIONS</subject><subject>ENERGY</subject><subject>HEAT TREATMENTS</subject><subject>HYDROCARBONS</subject><subject>INORGANIC, ORGANIC, PHYSICAL AND ANALYTICAL CHEMISTRY</subject><subject>ISOMERIZATION</subject><subject>KINETICS</subject><subject>MOLYBDENUM COMPOUNDS</subject><subject>MOLYBDENUM OXIDES</subject><subject>ORGANIC COMPOUNDS</subject><subject>OXIDES</subject><subject>OXYGEN COMPOUNDS</subject><subject>PRECURSOR</subject><subject>PROPYLENE</subject><subject>REACTION KINETICS</subject><subject>REDUCTION</subject><subject>REFRACTORY METAL COMPOUNDS</subject><subject>SURFACE PROPERTIES</subject><subject>TEMPERATURE RANGE</subject><subject>TEMPERATURE RANGE 0400-1000 K</subject><subject>TEMPERATURE RANGE 1000-4000 K</subject><subject>TRANSITION ELEMENT COMPOUNDS</subject><subject>VALENCE</subject><issn>0021-9517</issn><issn>1090-2694</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1992</creationdate><recordtype>article</recordtype><recordid>eNqNjL1qAkEUhQeJ4EbzBikuVqbY9c5sdnVKkYgWIoqdiEzGkZ2w2SnuVfARfGvFv9rqHA7fd4T4lJhIlHkXUclYZ7LX0epLo-rn8bwmIokaY5Xr7zcRPZGGeCf6Q5Qyy_qROC3cdm_ZhwpMtYV_x4YLR57AXNaD5yOEHUzDbEX7X0jX3UF5bWr9WMAaNuWRmBKYTBJYFu7mmuvry3ZL1HemJPdxz6Zoj36Ww3EciP2GrGdnCxuqylne5LqXaZWmL0FntEhYYg</recordid><startdate>19920501</startdate><enddate>19920501</enddate><creator>Gruenert, W.</creator><creator>Feldhaus, R.</creator><creator>Anders, K.</creator><creator>Stakheev, A.Y.</creator><creator>Shpiro, E.S.</creator><creator>Minachev, K.M.</creator><scope>OTOTI</scope></search><sort><creationdate>19920501</creationdate><title>Reduction and metathesis activity of MoO[sub 3]/Al[sub 2]O[sub 3] catalysts. II. The activation of MoO[sub 3]/Al[sub 2]O[sub 3] catalysts</title><author>Gruenert, W. ; Feldhaus, R. ; Anders, K. ; Stakheev, A.Y. ; Shpiro, E.S. ; Minachev, K.M.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-osti_scitechconnect_69759233</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1992</creationdate><topic>02 PETROLEUM</topic><topic>020400 - Petroleum- Processing</topic><topic>400201 - Chemical & Physicochemical Properties</topic><topic>ACTIVATION ENERGY</topic><topic>ALKENES</topic><topic>ALUMINIUM COMPOUNDS</topic><topic>ALUMINIUM OXIDES</topic><topic>CATALYST SUPPORTS</topic><topic>CATALYSTS</topic><topic>CATALYTIC EFFECTS</topic><topic>CHALCOGENIDES</topic><topic>CHEMICAL ACTIVATION</topic><topic>CHEMICAL REACTION KINETICS</topic><topic>CHEMICAL REACTIONS</topic><topic>ENERGY</topic><topic>HEAT TREATMENTS</topic><topic>HYDROCARBONS</topic><topic>INORGANIC, ORGANIC, PHYSICAL AND ANALYTICAL CHEMISTRY</topic><topic>ISOMERIZATION</topic><topic>KINETICS</topic><topic>MOLYBDENUM COMPOUNDS</topic><topic>MOLYBDENUM OXIDES</topic><topic>ORGANIC COMPOUNDS</topic><topic>OXIDES</topic><topic>OXYGEN COMPOUNDS</topic><topic>PRECURSOR</topic><topic>PROPYLENE</topic><topic>REACTION KINETICS</topic><topic>REDUCTION</topic><topic>REFRACTORY METAL COMPOUNDS</topic><topic>SURFACE PROPERTIES</topic><topic>TEMPERATURE RANGE</topic><topic>TEMPERATURE RANGE 0400-1000 K</topic><topic>TEMPERATURE RANGE 1000-4000 K</topic><topic>TRANSITION ELEMENT COMPOUNDS</topic><topic>VALENCE</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Gruenert, W.</creatorcontrib><creatorcontrib>Feldhaus, R.</creatorcontrib><creatorcontrib>Anders, K.</creatorcontrib><creatorcontrib>Stakheev, A.Y.</creatorcontrib><creatorcontrib>Shpiro, E.S.</creatorcontrib><creatorcontrib>Minachev, K.M.</creatorcontrib><collection>OSTI.GOV</collection><jtitle>Journal of catalysis</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Gruenert, W.</au><au>Feldhaus, R.</au><au>Anders, K.</au><au>Stakheev, A.Y.</au><au>Shpiro, E.S.</au><au>Minachev, K.M.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Reduction and metathesis activity of MoO[sub 3]/Al[sub 2]O[sub 3] catalysts. II. The activation of MoO[sub 3]/Al[sub 2]O[sub 3] catalysts</atitle><jtitle>Journal of catalysis</jtitle><date>1992-05-01</date><risdate>1992</risdate><volume>135:1</volume><issn>0021-9517</issn><eissn>1090-2694</eissn><abstract>MoO[sub 3]/Al[sub 2]O[sub 3] catalysts (0.5-13 wt% MoO[sub 3]) were activated for the metathesis of propene by thermal treatment in flowing inert gas and by reduction in H[sub 2] (reaction conditions: 473 K, 0.1 MPa). Temperatures between 900 and 1140 K were applied for the activation of the catalysts in inert atmosphere. The activity of the supported Mo (molecules/s Mo) increased with decreasing MoO[sub 3] content, which is opposite to the well-known trends for the reducibility of Mo(VI)/Al[sub 2]O[sub 3]. The kinetic reaction order of the propene metathesis was found to be 0.8 at 473 K. The apparent activation energy was 30-37 kJ/mole, with a slight decrease at increasing MoO[sub 3] content. The response of the activity to the extent of reduction was investigated at different reduction temperatures and MoO[sub 3] contents. From these observations and the results of the thermal activation study, it has been concluded that the active sites of metathesis can be formed from both Mo(VI) and Mo(IV) precursors. These precursors coexist on reduced surfaces, while the activity attained after thermal activation in inert gas is due exclusively to sites originating from mo(VI) species. Other Mo states (Mo(V), and Mo(II), and MO(0)) do not contribute to the metathesis activity.</abstract><cop>United States</cop><doi>10.1016/0021-9517(92)90286-Q</doi></addata></record> |
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subjects | 02 PETROLEUM 020400 - Petroleum- Processing 400201 - Chemical & Physicochemical Properties ACTIVATION ENERGY ALKENES ALUMINIUM COMPOUNDS ALUMINIUM OXIDES CATALYST SUPPORTS CATALYSTS CATALYTIC EFFECTS CHALCOGENIDES CHEMICAL ACTIVATION CHEMICAL REACTION KINETICS CHEMICAL REACTIONS ENERGY HEAT TREATMENTS HYDROCARBONS INORGANIC, ORGANIC, PHYSICAL AND ANALYTICAL CHEMISTRY ISOMERIZATION KINETICS MOLYBDENUM COMPOUNDS MOLYBDENUM OXIDES ORGANIC COMPOUNDS OXIDES OXYGEN COMPOUNDS PRECURSOR PROPYLENE REACTION KINETICS REDUCTION REFRACTORY METAL COMPOUNDS SURFACE PROPERTIES TEMPERATURE RANGE TEMPERATURE RANGE 0400-1000 K TEMPERATURE RANGE 1000-4000 K TRANSITION ELEMENT COMPOUNDS VALENCE |
title | Reduction and metathesis activity of MoO[sub 3]/Al[sub 2]O[sub 3] catalysts. II. The activation of MoO[sub 3]/Al[sub 2]O[sub 3] catalysts |
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