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Fischer-Tropsch performance correlated to catalyst structure: Trends in activity and stability for a silica-supported cobalt catalyst
•Particle size and size distribution of Co Fischer-Tropsch (FT) catalysts was determined from XRD.•FT performance was measured at industrially relevant conditions (210°C, H2/CO=2, 20 bar).•FT turnover frequency increases linearly with Co0 particle size up to 9.8nm.•The breadth of the particle size d...
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Published in: | Applied catalysis. A, General General, 2013-08, Vol.464-465, p.200-206 |
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creator | Richard, Laura A. Moreau, Pierre Rugmini, Sreekala Daly, Francis |
description | •Particle size and size distribution of Co Fischer-Tropsch (FT) catalysts was determined from XRD.•FT performance was measured at industrially relevant conditions (210°C, H2/CO=2, 20 bar).•FT turnover frequency increases linearly with Co0 particle size up to 9.8nm.•The breadth of the particle size distribution correlates directly to FT stability.•We show an active catalyst with deactivation of −0.08% CO converted/day in a microchannel reactor.
The influence of the cobalt particle size and particle size distribution in determining Fischer-Tropsch (FT) performance for silica supported catalysts was investigated. Using a line broadening powder X-ray diffraction analysis, both the particle size and particle size distribution of cobalt were estimated and compared to the FT activity and stability at industrially relevant conditions (210°C, H2/CO=2, 20bar). It was shown that the apparent turnover frequency increased linearly with Co0 particle size up to 9.8nm, the largest size tested. For the first time, it has been shown that the breadth of the particle size distribution correlates directly to catalyst stability. Using these correlations, a highly active and stable catalyst was developed, showing a deactivation rate of −0.08% CO converted/day in a microchannel reactor with an activity of 0.25molCOgCo−1h−1. |
doi_str_mv | 10.1016/j.apcata.2013.05.047 |
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The influence of the cobalt particle size and particle size distribution in determining Fischer-Tropsch (FT) performance for silica supported catalysts was investigated. Using a line broadening powder X-ray diffraction analysis, both the particle size and particle size distribution of cobalt were estimated and compared to the FT activity and stability at industrially relevant conditions (210°C, H2/CO=2, 20bar). It was shown that the apparent turnover frequency increased linearly with Co0 particle size up to 9.8nm, the largest size tested. For the first time, it has been shown that the breadth of the particle size distribution correlates directly to catalyst stability. Using these correlations, a highly active and stable catalyst was developed, showing a deactivation rate of −0.08% CO converted/day in a microchannel reactor with an activity of 0.25molCOgCo−1h−1.</description><identifier>ISSN: 0926-860X</identifier><identifier>EISSN: 1873-3875</identifier><identifier>DOI: 10.1016/j.apcata.2013.05.047</identifier><language>eng</language><publisher>Kidlington: Elsevier B.V</publisher><subject>Carbon monoxide ; Catalysis ; Catalysts ; Chemistry ; Cobalt ; Correlation ; Exact sciences and technology ; Fischer-Tropsch ; General and physical chemistry ; Line broadening ; Particle size ; Particle size distribution ; Silica ; Stability ; Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry ; X-ray diffraction</subject><ispartof>Applied catalysis. A, General, 2013-08, Vol.464-465, p.200-206</ispartof><rights>2013 Elsevier B.V.</rights><rights>2014 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c406t-a0d22a756a5a5695edf2df31a17ae254d622f93cc531aaa22a70358b5d70f55e3</citedby><cites>FETCH-LOGICAL-c406t-a0d22a756a5a5695edf2df31a17ae254d622f93cc531aaa22a70358b5d70f55e3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,776,780,27901,27902</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=27627105$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Richard, Laura A.</creatorcontrib><creatorcontrib>Moreau, Pierre</creatorcontrib><creatorcontrib>Rugmini, Sreekala</creatorcontrib><creatorcontrib>Daly, Francis</creatorcontrib><title>Fischer-Tropsch performance correlated to catalyst structure: Trends in activity and stability for a silica-supported cobalt catalyst</title><title>Applied catalysis. A, General</title><description>•Particle size and size distribution of Co Fischer-Tropsch (FT) catalysts was determined from XRD.•FT performance was measured at industrially relevant conditions (210°C, H2/CO=2, 20 bar).•FT turnover frequency increases linearly with Co0 particle size up to 9.8nm.•The breadth of the particle size distribution correlates directly to FT stability.•We show an active catalyst with deactivation of −0.08% CO converted/day in a microchannel reactor.
The influence of the cobalt particle size and particle size distribution in determining Fischer-Tropsch (FT) performance for silica supported catalysts was investigated. Using a line broadening powder X-ray diffraction analysis, both the particle size and particle size distribution of cobalt were estimated and compared to the FT activity and stability at industrially relevant conditions (210°C, H2/CO=2, 20bar). It was shown that the apparent turnover frequency increased linearly with Co0 particle size up to 9.8nm, the largest size tested. For the first time, it has been shown that the breadth of the particle size distribution correlates directly to catalyst stability. Using these correlations, a highly active and stable catalyst was developed, showing a deactivation rate of −0.08% CO converted/day in a microchannel reactor with an activity of 0.25molCOgCo−1h−1.</description><subject>Carbon monoxide</subject><subject>Catalysis</subject><subject>Catalysts</subject><subject>Chemistry</subject><subject>Cobalt</subject><subject>Correlation</subject><subject>Exact sciences and technology</subject><subject>Fischer-Tropsch</subject><subject>General and physical chemistry</subject><subject>Line broadening</subject><subject>Particle size</subject><subject>Particle size distribution</subject><subject>Silica</subject><subject>Stability</subject><subject>Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry</subject><subject>X-ray diffraction</subject><issn>0926-860X</issn><issn>1873-3875</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2013</creationdate><recordtype>article</recordtype><recordid>eNp9kMGKFDEQhoMoOK6-gYdcBC_dJulOMu1BkMVVYcHLCN5CTVKNGXo6bSW9MA_ge5tmlj16Sqr46i_qY-ytFK0U0nw4tbB4KNAqIbtW6Fb09hnbyb3tmm5v9XO2E4Myzd6IXy_Zq5xPQgjVD3rH_t7F7H8jNQdKS_3xBWlMdIbZI_eJCCcoGHhJfNswXXLhudDqy0r4kR8I55B5nDn4Eh9iuXCYQyXgGKetqlkceK6Fhyavy5Joi_PpCFN5inzNXowwZXzz-N6wn3dfDrffmvsfX7_ffr5vfC9MaUAEpcBqAxq0GTSGUYWxkyAtoNJ9MEqNQ-e9rj2AjRWd3h91sGLUGrsb9v6au1D6s2Iu7lzPx2mCGdOanexNr7W0_VDR_op6SjkTjm6heAa6OCncZt2d3NW626w7oV21XsfePW6A7GEaqYqM-WlWWaOsFLpyn64c1nMfIpLLPmKVHiKhLy6k-P9F_wDHI51T</recordid><startdate>20130815</startdate><enddate>20130815</enddate><creator>Richard, Laura A.</creator><creator>Moreau, Pierre</creator><creator>Rugmini, Sreekala</creator><creator>Daly, Francis</creator><general>Elsevier B.V</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>7TB</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>FR3</scope><scope>JG9</scope><scope>L7M</scope></search><sort><creationdate>20130815</creationdate><title>Fischer-Tropsch performance correlated to catalyst structure: Trends in activity and stability for a silica-supported cobalt catalyst</title><author>Richard, Laura A. ; Moreau, Pierre ; Rugmini, Sreekala ; Daly, Francis</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c406t-a0d22a756a5a5695edf2df31a17ae254d622f93cc531aaa22a70358b5d70f55e3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2013</creationdate><topic>Carbon monoxide</topic><topic>Catalysis</topic><topic>Catalysts</topic><topic>Chemistry</topic><topic>Cobalt</topic><topic>Correlation</topic><topic>Exact sciences and technology</topic><topic>Fischer-Tropsch</topic><topic>General and physical chemistry</topic><topic>Line broadening</topic><topic>Particle size</topic><topic>Particle size distribution</topic><topic>Silica</topic><topic>Stability</topic><topic>Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry</topic><topic>X-ray diffraction</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Richard, Laura A.</creatorcontrib><creatorcontrib>Moreau, Pierre</creatorcontrib><creatorcontrib>Rugmini, Sreekala</creatorcontrib><creatorcontrib>Daly, Francis</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Materials Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Applied catalysis. A, General</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Richard, Laura A.</au><au>Moreau, Pierre</au><au>Rugmini, Sreekala</au><au>Daly, Francis</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Fischer-Tropsch performance correlated to catalyst structure: Trends in activity and stability for a silica-supported cobalt catalyst</atitle><jtitle>Applied catalysis. A, General</jtitle><date>2013-08-15</date><risdate>2013</risdate><volume>464-465</volume><spage>200</spage><epage>206</epage><pages>200-206</pages><issn>0926-860X</issn><eissn>1873-3875</eissn><abstract>•Particle size and size distribution of Co Fischer-Tropsch (FT) catalysts was determined from XRD.•FT performance was measured at industrially relevant conditions (210°C, H2/CO=2, 20 bar).•FT turnover frequency increases linearly with Co0 particle size up to 9.8nm.•The breadth of the particle size distribution correlates directly to FT stability.•We show an active catalyst with deactivation of −0.08% CO converted/day in a microchannel reactor.
The influence of the cobalt particle size and particle size distribution in determining Fischer-Tropsch (FT) performance for silica supported catalysts was investigated. Using a line broadening powder X-ray diffraction analysis, both the particle size and particle size distribution of cobalt were estimated and compared to the FT activity and stability at industrially relevant conditions (210°C, H2/CO=2, 20bar). It was shown that the apparent turnover frequency increased linearly with Co0 particle size up to 9.8nm, the largest size tested. For the first time, it has been shown that the breadth of the particle size distribution correlates directly to catalyst stability. Using these correlations, a highly active and stable catalyst was developed, showing a deactivation rate of −0.08% CO converted/day in a microchannel reactor with an activity of 0.25molCOgCo−1h−1.</abstract><cop>Kidlington</cop><pub>Elsevier B.V</pub><doi>10.1016/j.apcata.2013.05.047</doi><tpages>7</tpages></addata></record> |
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subjects | Carbon monoxide Catalysis Catalysts Chemistry Cobalt Correlation Exact sciences and technology Fischer-Tropsch General and physical chemistry Line broadening Particle size Particle size distribution Silica Stability Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry X-ray diffraction |
title | Fischer-Tropsch performance correlated to catalyst structure: Trends in activity and stability for a silica-supported cobalt catalyst |
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