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Mesoporous Chromium Catalysts Templated on Halloysite Nanotubes and Aluminosilicate Core/Shell Composites for Oxidative Dehydrogenation of Propane with CO2
The oxidative dehydrogenation of alkanes is a prospective method for olefins production. CO2-assisted propane dehydrogenation over metal oxide catalysts provides an opportunity to increase propylene production with collateral CO2 utilization. We prepared the chromia catalysts on various mesoporous a...
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Published in: | Catalysts 2023-05, Vol.13 (5), p.882 |
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description | The oxidative dehydrogenation of alkanes is a prospective method for olefins production. CO2-assisted propane dehydrogenation over metal oxide catalysts provides an opportunity to increase propylene production with collateral CO2 utilization. We prepared the chromia catalysts on various mesoporous aluminosilicate supports, such as halloysite nanotubes, nanostructured core/shell composites of MCM-41/halloysite (halloysite nanotubes for the core; silica of MCM-41-type for the shell), and MCM-41@halloysite (silica of MCM-41-type for the core; halloysite nanotubes for the shell). The catalysts have been characterized by X-ray fluorescence analysis, low-temperature nitrogen adsorption, X-ray diffraction, temperature-programmed reduction, temperature-programmed desorption of ammonia, transmission electron microscopy with energy-dispersive X-ray spectroscopy, and thermogravimetric analysis. The catalysts’ performance in carbon-dioxide-assisted propane dehydrogenation has been estimated in a fixed-bed reactor at atmospheric pressure. The most stable catalyst is Cr/halloysite, having the lowest activity and the largest pore diameter. The catalyst, Cr/MCM-41/HNT, shows the best catalytic performance: having the highest conversion (19–88%), selectivity (83–30%), and space–time yield (4.3–7.1 mol C3H6/kg catalyst/h) at the temperature range of 550–700 °C. The highest space–time yield could be related to the uniform distribution of the chromia particles over the large surface area and narrow pore size distribution of 2–4 nm provided by the MCM-41-type silica and transport channels of 12–15 nm from the halloysite nanotubes. |
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CO2-assisted propane dehydrogenation over metal oxide catalysts provides an opportunity to increase propylene production with collateral CO2 utilization. We prepared the chromia catalysts on various mesoporous aluminosilicate supports, such as halloysite nanotubes, nanostructured core/shell composites of MCM-41/halloysite (halloysite nanotubes for the core; silica of MCM-41-type for the shell), and MCM-41@halloysite (silica of MCM-41-type for the core; halloysite nanotubes for the shell). The catalysts have been characterized by X-ray fluorescence analysis, low-temperature nitrogen adsorption, X-ray diffraction, temperature-programmed reduction, temperature-programmed desorption of ammonia, transmission electron microscopy with energy-dispersive X-ray spectroscopy, and thermogravimetric analysis. The catalysts’ performance in carbon-dioxide-assisted propane dehydrogenation has been estimated in a fixed-bed reactor at atmospheric pressure. The most stable catalyst is Cr/halloysite, having the lowest activity and the largest pore diameter. The catalyst, Cr/MCM-41/HNT, shows the best catalytic performance: having the highest conversion (19–88%), selectivity (83–30%), and space–time yield (4.3–7.1 mol C3H6/kg catalyst/h) at the temperature range of 550–700 °C. The highest space–time yield could be related to the uniform distribution of the chromia particles over the large surface area and narrow pore size distribution of 2–4 nm provided by the MCM-41-type silica and transport channels of 12–15 nm from the halloysite nanotubes.</description><identifier>ISSN: 2073-4344</identifier><identifier>EISSN: 2073-4344</identifier><identifier>DOI: 10.3390/catal13050882</identifier><language>eng</language><publisher>Basel: MDPI AG</publisher><subject>Alkanes ; Alkenes ; aluminosilicate ; Aluminosilicates ; Aluminum silicates ; Ammonia ; Carbon dioxide ; Catalysts ; Catalytic converters ; Catalytic cracking ; Chemical reactions ; Chromium oxides ; Composite materials ; Dehydrogenation ; Hydrocarbons ; Investigations ; Low temperature ; Mechanical properties ; mesoporous materials ; mesoporous silica ; Metal oxides ; Nanotubes ; Natural gas ; oxidative dehydrogenation ; Pore size distribution ; Propane ; Propylene ; Silica ; Silicon dioxide ; Thermogravimetric analysis ; X ray fluorescence analysis ; Zeolites</subject><ispartof>Catalysts, 2023-05, Vol.13 (5), p.882</ispartof><rights>2023 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (https://creativecommons.org/licenses/by/4.0/). Notwithstanding the ProQuest Terms and Conditions, you may use this content in accordance with the terms of the License.</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c370t-707a7ad2cd24a264e44bc941600948cbbd9e6b6ea35035772afd98cd217257a83</citedby><cites>FETCH-LOGICAL-c370t-707a7ad2cd24a264e44bc941600948cbbd9e6b6ea35035772afd98cd217257a83</cites><orcidid>0000-0002-0887-6678 ; 0000-0002-0570-6577 ; 0000-0001-6529-2321 ; 0000-0002-2877-0395</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://www.proquest.com/docview/2819403875/fulltextPDF?pq-origsite=primo$$EPDF$$P50$$Gproquest$$Hfree_for_read</linktopdf><linktohtml>$$Uhttps://www.proquest.com/docview/2819403875?pq-origsite=primo$$EHTML$$P50$$Gproquest$$Hfree_for_read</linktohtml><link.rule.ids>314,780,784,25753,27924,27925,37012,44590,74998</link.rule.ids></links><search><creatorcontrib>Melnikov, Dmitry</creatorcontrib><creatorcontrib>Smirnova, Ekaterina</creatorcontrib><creatorcontrib>Reshetina, Marina</creatorcontrib><creatorcontrib>Novikov, Andrei</creatorcontrib><creatorcontrib>Wang, Hongqiang</creatorcontrib><creatorcontrib>Ivanov, Evgenii</creatorcontrib><creatorcontrib>Vinokurov, Vladimir</creatorcontrib><creatorcontrib>Glotov, Aleksandr</creatorcontrib><title>Mesoporous Chromium Catalysts Templated on Halloysite Nanotubes and Aluminosilicate Core/Shell Composites for Oxidative Dehydrogenation of Propane with CO2</title><title>Catalysts</title><description>The oxidative dehydrogenation of alkanes is a prospective method for olefins production. CO2-assisted propane dehydrogenation over metal oxide catalysts provides an opportunity to increase propylene production with collateral CO2 utilization. We prepared the chromia catalysts on various mesoporous aluminosilicate supports, such as halloysite nanotubes, nanostructured core/shell composites of MCM-41/halloysite (halloysite nanotubes for the core; silica of MCM-41-type for the shell), and MCM-41@halloysite (silica of MCM-41-type for the core; halloysite nanotubes for the shell). The catalysts have been characterized by X-ray fluorescence analysis, low-temperature nitrogen adsorption, X-ray diffraction, temperature-programmed reduction, temperature-programmed desorption of ammonia, transmission electron microscopy with energy-dispersive X-ray spectroscopy, and thermogravimetric analysis. The catalysts’ performance in carbon-dioxide-assisted propane dehydrogenation has been estimated in a fixed-bed reactor at atmospheric pressure. The most stable catalyst is Cr/halloysite, having the lowest activity and the largest pore diameter. The catalyst, Cr/MCM-41/HNT, shows the best catalytic performance: having the highest conversion (19–88%), selectivity (83–30%), and space–time yield (4.3–7.1 mol C3H6/kg catalyst/h) at the temperature range of 550–700 °C. The highest space–time yield could be related to the uniform distribution of the chromia particles over the large surface area and narrow pore size distribution of 2–4 nm provided by the MCM-41-type silica and transport channels of 12–15 nm from the halloysite nanotubes.</description><subject>Alkanes</subject><subject>Alkenes</subject><subject>aluminosilicate</subject><subject>Aluminosilicates</subject><subject>Aluminum silicates</subject><subject>Ammonia</subject><subject>Carbon dioxide</subject><subject>Catalysts</subject><subject>Catalytic converters</subject><subject>Catalytic cracking</subject><subject>Chemical reactions</subject><subject>Chromium oxides</subject><subject>Composite materials</subject><subject>Dehydrogenation</subject><subject>Hydrocarbons</subject><subject>Investigations</subject><subject>Low temperature</subject><subject>Mechanical properties</subject><subject>mesoporous materials</subject><subject>mesoporous silica</subject><subject>Metal oxides</subject><subject>Nanotubes</subject><subject>Natural gas</subject><subject>oxidative dehydrogenation</subject><subject>Pore size distribution</subject><subject>Propane</subject><subject>Propylene</subject><subject>Silica</subject><subject>Silicon dioxide</subject><subject>Thermogravimetric analysis</subject><subject>X ray fluorescence analysis</subject><subject>Zeolites</subject><issn>2073-4344</issn><issn>2073-4344</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2023</creationdate><recordtype>article</recordtype><sourceid>PIMPY</sourceid><sourceid>DOA</sourceid><recordid>eNpVkUtv1DAQxyMEElXpkbslzkv9yto5VuHRSoVFopyjiTPpeuVkgu0A-1n4snhZhGAu89B_fjOjqaqXgr9WquHXDjIEoXjNrZVPqgvJjdpopfXTf-Ln1VVKB16sEcqK-qL6-QETLRRpTazdR5r8OrH2xDqmnNgDTkuAjAOjmd1CCHRMPiP7CDPltcfEYB7YTVgnP1PywZc1kLUU8frzHkMo4bTQqSWxkSLb_fADZP8N2RvcH4dIjziXvMBpZJ8iLTAj--7znrU7-aJ6NkJIePXHX1Zf3r19aG8397v3d-3N_cYpw_PGcAMGBukGqUFuNWrdu0aLbblSW9f3Q4Pbfougaq5qYySMQ2OLWhhZG7Dqsro7cweCQ7dEP0E8dgS--12g-NhBzN4F7IQyeqxt0wAKrcDZxhh0vRi1ka6XprBenVlLpK8rptwdaI1zWb-TVjSaK2vqotqcVS5SShHHv1MF707v7P57p_oF3KaViA</recordid><startdate>20230513</startdate><enddate>20230513</enddate><creator>Melnikov, Dmitry</creator><creator>Smirnova, Ekaterina</creator><creator>Reshetina, Marina</creator><creator>Novikov, Andrei</creator><creator>Wang, Hongqiang</creator><creator>Ivanov, Evgenii</creator><creator>Vinokurov, Vladimir</creator><creator>Glotov, Aleksandr</creator><general>MDPI AG</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>8BQ</scope><scope>8FD</scope><scope>8FE</scope><scope>8FG</scope><scope>ABJCF</scope><scope>ABUWG</scope><scope>AFKRA</scope><scope>AZQEC</scope><scope>BENPR</scope><scope>BGLVJ</scope><scope>CCPQU</scope><scope>D1I</scope><scope>DWQXO</scope><scope>HCIFZ</scope><scope>JG9</scope><scope>KB.</scope><scope>PDBOC</scope><scope>PIMPY</scope><scope>PQEST</scope><scope>PQQKQ</scope><scope>PQUKI</scope><scope>PRINS</scope><scope>DOA</scope><orcidid>https://orcid.org/0000-0002-0887-6678</orcidid><orcidid>https://orcid.org/0000-0002-0570-6577</orcidid><orcidid>https://orcid.org/0000-0001-6529-2321</orcidid><orcidid>https://orcid.org/0000-0002-2877-0395</orcidid></search><sort><creationdate>20230513</creationdate><title>Mesoporous Chromium Catalysts Templated on Halloysite Nanotubes and Aluminosilicate Core/Shell Composites for Oxidative Dehydrogenation of Propane with CO2</title><author>Melnikov, Dmitry ; 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CO2-assisted propane dehydrogenation over metal oxide catalysts provides an opportunity to increase propylene production with collateral CO2 utilization. We prepared the chromia catalysts on various mesoporous aluminosilicate supports, such as halloysite nanotubes, nanostructured core/shell composites of MCM-41/halloysite (halloysite nanotubes for the core; silica of MCM-41-type for the shell), and MCM-41@halloysite (silica of MCM-41-type for the core; halloysite nanotubes for the shell). The catalysts have been characterized by X-ray fluorescence analysis, low-temperature nitrogen adsorption, X-ray diffraction, temperature-programmed reduction, temperature-programmed desorption of ammonia, transmission electron microscopy with energy-dispersive X-ray spectroscopy, and thermogravimetric analysis. The catalysts’ performance in carbon-dioxide-assisted propane dehydrogenation has been estimated in a fixed-bed reactor at atmospheric pressure. The most stable catalyst is Cr/halloysite, having the lowest activity and the largest pore diameter. The catalyst, Cr/MCM-41/HNT, shows the best catalytic performance: having the highest conversion (19–88%), selectivity (83–30%), and space–time yield (4.3–7.1 mol C3H6/kg catalyst/h) at the temperature range of 550–700 °C. The highest space–time yield could be related to the uniform distribution of the chromia particles over the large surface area and narrow pore size distribution of 2–4 nm provided by the MCM-41-type silica and transport channels of 12–15 nm from the halloysite nanotubes.</abstract><cop>Basel</cop><pub>MDPI AG</pub><doi>10.3390/catal13050882</doi><orcidid>https://orcid.org/0000-0002-0887-6678</orcidid><orcidid>https://orcid.org/0000-0002-0570-6577</orcidid><orcidid>https://orcid.org/0000-0001-6529-2321</orcidid><orcidid>https://orcid.org/0000-0002-2877-0395</orcidid><oa>free_for_read</oa></addata></record> |
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subjects | Alkanes Alkenes aluminosilicate Aluminosilicates Aluminum silicates Ammonia Carbon dioxide Catalysts Catalytic converters Catalytic cracking Chemical reactions Chromium oxides Composite materials Dehydrogenation Hydrocarbons Investigations Low temperature Mechanical properties mesoporous materials mesoporous silica Metal oxides Nanotubes Natural gas oxidative dehydrogenation Pore size distribution Propane Propylene Silica Silicon dioxide Thermogravimetric analysis X ray fluorescence analysis Zeolites |
title | Mesoporous Chromium Catalysts Templated on Halloysite Nanotubes and Aluminosilicate Core/Shell Composites for Oxidative Dehydrogenation of Propane with CO2 |
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