Controlling the Evolution of Active Molybdenum Carbide by Moderating the Acidity of Mo/HMCM-22 Catalyst in Methane Dehydroaromatization

Effect of framework Brønsted Acidity by varying SiO 2 /Al 2 O 3 ratio (SAR) of HMCM-22 zeolite is studied with respect to the formation of active molybdenum carbide and its anchoring over zeolite (HMCM-22) channels of Mo/HMCM-22 catalyst tested for methane dehydroaromatization (MDA) reaction. For th...

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Veröffentlicht in:Catalysis letters 2020-12, Vol.150 (12), p.3653-3666
Hauptverfasser: Mishra, Sourabh, Ali Haider, M., Pant, K. K.
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description Effect of framework Brønsted Acidity by varying SiO 2 /Al 2 O 3 ratio (SAR) of HMCM-22 zeolite is studied with respect to the formation of active molybdenum carbide and its anchoring over zeolite (HMCM-22) channels of Mo/HMCM-22 catalyst tested for methane dehydroaromatization (MDA) reaction. For this purpose, HMCM-22 is synthesized by conventional methods with varying SAR (30, 40 & 55) and is studied for MDA reaction with 5 wt% Mo loading. XRD, BET, NH 3 -TPD, H 2 -TPR, 27 Al MAS NMR, Raman spectroscopy and XPS techniques are used to characterize 5Mo/HMCM-22 catalyst having different SAR. XPS analysis of carburized 5Mo/HMCM-22 (SAR-30, 40 & 55) catalyst confirms that higher content of molybdenum carbide (Mo 2 C) forms over HMCM-22 channels at SAR-30 as compared to SAR-40 and SAR-55 due to effective binding of initial MoO x species. Interaction of initial MoO x species with HMCM-22 zeolite framework is analyzed using 27 Al MAS NMR and Raman spectroscopic studies which confirm that MoO x species bind differently at SAR-30, 40 and 55 which affects the catalytic performance. Lower reducibility of MoO x species at SAR-30 confirms that MoO x species strongly interact with HMCM-22 channels at SAR-30 as confirmed by H 2 -TPR study. Maximum transformation of MoO x species into active molybdenum carbide over HMCM-22 at lower SAR (30) during carburization results in higher activity of 5Mo/HMCM-22 (SAR-30) catalyst with lower coke content. Graphic Abstract
doi_str_mv 10.1007/s10562-020-03269-x
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Interaction of initial MoO x species with HMCM-22 zeolite framework is analyzed using 27 Al MAS NMR and Raman spectroscopic studies which confirm that MoO x species bind differently at SAR-30, 40 and 55 which affects the catalytic performance. Lower reducibility of MoO x species at SAR-30 confirms that MoO x species strongly interact with HMCM-22 channels at SAR-30 as confirmed by H 2 -TPR study. Maximum transformation of MoO x species into active molybdenum carbide over HMCM-22 at lower SAR (30) during carburization results in higher activity of 5Mo/HMCM-22 (SAR-30) catalyst with lower coke content. 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K.</creatorcontrib><title>Controlling the Evolution of Active Molybdenum Carbide by Moderating the Acidity of Mo/HMCM-22 Catalyst in Methane Dehydroaromatization</title><title>Catalysis letters</title><addtitle>Catal Lett</addtitle><description>Effect of framework Brønsted Acidity by varying SiO 2 /Al 2 O 3 ratio (SAR) of HMCM-22 zeolite is studied with respect to the formation of active molybdenum carbide and its anchoring over zeolite (HMCM-22) channels of Mo/HMCM-22 catalyst tested for methane dehydroaromatization (MDA) reaction. For this purpose, HMCM-22 is synthesized by conventional methods with varying SAR (30, 40 &amp; 55) and is studied for MDA reaction with 5 wt% Mo loading. XRD, BET, NH 3 -TPD, H 2 -TPR, 27 Al MAS NMR, Raman spectroscopy and XPS techniques are used to characterize 5Mo/HMCM-22 catalyst having different SAR. XPS analysis of carburized 5Mo/HMCM-22 (SAR-30, 40 &amp; 55) catalyst confirms that higher content of molybdenum carbide (Mo 2 C) forms over HMCM-22 channels at SAR-30 as compared to SAR-40 and SAR-55 due to effective binding of initial MoO x species. Interaction of initial MoO x species with HMCM-22 zeolite framework is analyzed using 27 Al MAS NMR and Raman spectroscopic studies which confirm that MoO x species bind differently at SAR-30, 40 and 55 which affects the catalytic performance. Lower reducibility of MoO x species at SAR-30 confirms that MoO x species strongly interact with HMCM-22 channels at SAR-30 as confirmed by H 2 -TPR study. Maximum transformation of MoO x species into active molybdenum carbide over HMCM-22 at lower SAR (30) during carburization results in higher activity of 5Mo/HMCM-22 (SAR-30) catalyst with lower coke content. 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K.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c401t-68e4b0d43e4ef9c0daafcd587f19075f4fec0b98bc097bb99fd275b9523720ff3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2020</creationdate><topic>Catalysis</topic><topic>Chemistry</topic><topic>Chemistry and Materials Science</topic><topic>Hydrogen-ion concentration</topic><topic>Industrial Chemistry/Chemical Engineering</topic><topic>Methane</topic><topic>Molybdenum</topic><topic>Nuclear magnetic resonance spectroscopy</topic><topic>Organometallic Chemistry</topic><topic>Physical Chemistry</topic><topic>Raman spectroscopy</topic><topic>Zeolites</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Mishra, Sourabh</creatorcontrib><creatorcontrib>Ali Haider, M.</creatorcontrib><creatorcontrib>Pant, K. 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K.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Controlling the Evolution of Active Molybdenum Carbide by Moderating the Acidity of Mo/HMCM-22 Catalyst in Methane Dehydroaromatization</atitle><jtitle>Catalysis letters</jtitle><stitle>Catal Lett</stitle><date>2020-12-01</date><risdate>2020</risdate><volume>150</volume><issue>12</issue><spage>3653</spage><epage>3666</epage><pages>3653-3666</pages><issn>1011-372X</issn><eissn>1572-879X</eissn><abstract>Effect of framework Brønsted Acidity by varying SiO 2 /Al 2 O 3 ratio (SAR) of HMCM-22 zeolite is studied with respect to the formation of active molybdenum carbide and its anchoring over zeolite (HMCM-22) channels of Mo/HMCM-22 catalyst tested for methane dehydroaromatization (MDA) reaction. For this purpose, HMCM-22 is synthesized by conventional methods with varying SAR (30, 40 &amp; 55) and is studied for MDA reaction with 5 wt% Mo loading. XRD, BET, NH 3 -TPD, H 2 -TPR, 27 Al MAS NMR, Raman spectroscopy and XPS techniques are used to characterize 5Mo/HMCM-22 catalyst having different SAR. XPS analysis of carburized 5Mo/HMCM-22 (SAR-30, 40 &amp; 55) catalyst confirms that higher content of molybdenum carbide (Mo 2 C) forms over HMCM-22 channels at SAR-30 as compared to SAR-40 and SAR-55 due to effective binding of initial MoO x species. Interaction of initial MoO x species with HMCM-22 zeolite framework is analyzed using 27 Al MAS NMR and Raman spectroscopic studies which confirm that MoO x species bind differently at SAR-30, 40 and 55 which affects the catalytic performance. Lower reducibility of MoO x species at SAR-30 confirms that MoO x species strongly interact with HMCM-22 channels at SAR-30 as confirmed by H 2 -TPR study. Maximum transformation of MoO x species into active molybdenum carbide over HMCM-22 at lower SAR (30) during carburization results in higher activity of 5Mo/HMCM-22 (SAR-30) catalyst with lower coke content. Graphic Abstract</abstract><cop>New York</cop><pub>Springer US</pub><doi>10.1007/s10562-020-03269-x</doi><tpages>14</tpages></addata></record>
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subjects Catalysis
Chemistry
Chemistry and Materials Science
Hydrogen-ion concentration
Industrial Chemistry/Chemical Engineering
Methane
Molybdenum
Nuclear magnetic resonance spectroscopy
Organometallic Chemistry
Physical Chemistry
Raman spectroscopy
Zeolites
title Controlling the Evolution of Active Molybdenum Carbide by Moderating the Acidity of Mo/HMCM-22 Catalyst in Methane Dehydroaromatization
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