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A Kinetic Model of Methanol Synthesis
A kinetic model of methanol synthesis is presented. All parameters in the model are estimated from gas-phase thermodynamics and surface science studies. The rate-limiting step in the kinetic model was determined from Cu(100) single-crystal experiments Ito be the hydrogenation of H2COO ☆ to methoxide...
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Published in: | Journal of catalysis 1995-10, Vol.156 (2), p.229-242 |
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Language: | English |
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container_end_page | 242 |
container_issue | 2 |
container_start_page | 229 |
container_title | Journal of catalysis |
container_volume | 156 |
creator | Askgaard, T.S. Norskov, J.K. Ovesen, C.V. Stoltze, P. |
description | A kinetic model of methanol synthesis is presented. All parameters in the model are estimated from gas-phase thermodynamics and surface science studies. The rate-limiting step in the kinetic model was determined from Cu(100) single-crystal experiments Ito be the hydrogenation of H2COO ☆ to methoxide and oxide. Calculated methanol rates from the model extrapolated to industrial working conditions were in good agreement with rates measured on a real catalyst. |
doi_str_mv | 10.1006/jcat.1995.1250 |
format | article |
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All parameters in the model are estimated from gas-phase thermodynamics and surface science studies. The rate-limiting step in the kinetic model was determined from Cu(100) single-crystal experiments Ito be the hydrogenation of H2COO ☆ to methoxide and oxide. Calculated methanol rates from the model extrapolated to industrial working conditions were in good agreement with rates measured on a real catalyst.</description><identifier>ISSN: 0021-9517</identifier><identifier>EISSN: 1090-2694</identifier><identifier>DOI: 10.1006/jcat.1995.1250</identifier><identifier>CODEN: JCTLA5</identifier><language>eng</language><publisher>Amsterdam: Elsevier Inc</publisher><subject>Catalysis ; Catalytic reactions ; Chemistry ; Exact sciences and technology ; General and physical chemistry ; Theory of reactions, general kinetics. Catalysis. 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All parameters in the model are estimated from gas-phase thermodynamics and surface science studies. The rate-limiting step in the kinetic model was determined from Cu(100) single-crystal experiments Ito be the hydrogenation of H2COO ☆ to methoxide and oxide. Calculated methanol rates from the model extrapolated to industrial working conditions were in good agreement with rates measured on a real catalyst.</description><subject>Catalysis</subject><subject>Catalytic reactions</subject><subject>Chemistry</subject><subject>Exact sciences and technology</subject><subject>General and physical chemistry</subject><subject>Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry</subject><issn>0021-9517</issn><issn>1090-2694</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1995</creationdate><recordtype>article</recordtype><recordid>eNp1jztPwzAUhS0EEqWwMmeAMeHexPFjrCpeohUDMFuufa26CkllR0j8exoVsTGd5Xz3no-xa4QKAcTdztmxQq3bCusWTtgMQUNZC81P2QygxlK3KM_ZRc47AMS2VTN2uyheYk9jdMV68NQVQyjWNG5tP3TF23c_binHfMnOgu0yXf3mnH083L8vn8rV6-PzcrEqXSPlWHohRPDkw4YTF6rWwUofUKOGlpTWClFuQisCR_CAApE4cKnqhoJ21jVzVh3vujTknCiYfYqfNn0bBDNJmknSTJJmkjwAN0dgb7OzXUi2dzH_UY3QqubyUFPHGh3Gf0VKJrtIvSMfE7nR-CH-9-EH5kNjhQ</recordid><startdate>19951001</startdate><enddate>19951001</enddate><creator>Askgaard, T.S.</creator><creator>Norskov, J.K.</creator><creator>Ovesen, C.V.</creator><creator>Stoltze, P.</creator><general>Elsevier Inc</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>19951001</creationdate><title>A Kinetic Model of Methanol Synthesis</title><author>Askgaard, T.S. ; Norskov, J.K. ; Ovesen, C.V. ; Stoltze, P.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c377t-d666fdedfb4e46829fa7df191905e8998117bf56f410d01611e4047823ef9cac3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1995</creationdate><topic>Catalysis</topic><topic>Catalytic reactions</topic><topic>Chemistry</topic><topic>Exact sciences and technology</topic><topic>General and physical chemistry</topic><topic>Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Askgaard, T.S.</creatorcontrib><creatorcontrib>Norskov, J.K.</creatorcontrib><creatorcontrib>Ovesen, C.V.</creatorcontrib><creatorcontrib>Stoltze, P.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><jtitle>Journal of catalysis</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Askgaard, T.S.</au><au>Norskov, J.K.</au><au>Ovesen, C.V.</au><au>Stoltze, P.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>A Kinetic Model of Methanol Synthesis</atitle><jtitle>Journal of catalysis</jtitle><date>1995-10-01</date><risdate>1995</risdate><volume>156</volume><issue>2</issue><spage>229</spage><epage>242</epage><pages>229-242</pages><issn>0021-9517</issn><eissn>1090-2694</eissn><coden>JCTLA5</coden><abstract>A kinetic model of methanol synthesis is presented. All parameters in the model are estimated from gas-phase thermodynamics and surface science studies. The rate-limiting step in the kinetic model was determined from Cu(100) single-crystal experiments Ito be the hydrogenation of H2COO ☆ to methoxide and oxide. Calculated methanol rates from the model extrapolated to industrial working conditions were in good agreement with rates measured on a real catalyst.</abstract><cop>Amsterdam</cop><pub>Elsevier Inc</pub><doi>10.1006/jcat.1995.1250</doi><tpages>14</tpages></addata></record> |
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subjects | Catalysis Catalytic reactions Chemistry Exact sciences and technology General and physical chemistry Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry |
title | A Kinetic Model of Methanol Synthesis |
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