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   <dc:title>Selective Metathesis of α-Olefins from Bio-Sourced Fischer–Tropsch Feeds</dc:title>
   <dc:creator>Rouen, Mathieu</dc:creator>
   <dc:creator>Queval, Pierre</dc:creator>
   <dc:creator>Borré, Etienne</dc:creator>
   <dc:creator>Falivene, Laura</dc:creator>
   <dc:creator>Poater Teixidor, Albert</dc:creator>
   <dc:creator>Berthod, Mikaël</dc:creator>
   <dc:creator>Hugues, François</dc:creator>
   <dc:creator>Cavallo, Luigi</dc:creator>
   <dc:creator>Baslé, Olivier</dc:creator>
   <dc:creator>Olivier-Bourbigou, Hélène</dc:creator>
   <dc:creator>Mauduit, Marc</dc:creator>
   <dc:subject>Fischer-Tropsch, Procés</dc:subject>
   <dc:subject>Fischer-Tropsch process</dc:subject>
   <dc:subject>Isomerització</dc:subject>
   <dc:subject>Isomerization</dc:subject>
   <dc:subject>Metàtesi (Química)</dc:subject>
   <dc:subject>Metathesis (Chemistry)</dc:subject>
   <dc:subject>Alquens</dc:subject>
   <dc:subject>Alkenes</dc:subject>
   <dcterms:abstract>The search for a low-cost process for the valorization of linear α-olefins combining high productivity and high selectivity is a longstanding goal for chemists. Herein, we report a soluble ruthenium olefin metathesis catalyst that performs the conversion of linear α-olefins to longer internal linear olefins with high selectivity (>99%) under neat conditions at low loadings (50 ppm) and without the need of expensive additives. This robust catalytic process allowed us to efficiently and selectively re-equilibrate the naphtha fraction (C5–C8) of a Fischer–Tropsch feed derived from non-petroleum resources to a higher-value product range (C9–C14), useful as detergent and plasticizer precursors</dcterms:abstract>
   <dcterms:abstract>This work was supported by the European Community through the seventh framework program (CP-FP 211468-2 EUMET, grant to M.R., L.F., and E.B.). M.M. thanks the CNRS, the ENSCR, Rennes Métropole, and the Région-Bretagne for their financial support. A.P. thanks the Spanish MINECO for project CTQ2014- 59832-JIN, and L.C. acknowledges funding from the King Abdullah University of Science and Technology (KAUST)</dcterms:abstract>
   <dcterms:dateAccepted>2024-06-18T13:52:57Z</dcterms:dateAccepted>
   <dcterms:available>2024-06-18T13:52:57Z</dcterms:available>
   <dcterms:created>2024-06-18T13:52:57Z</dcterms:created>
   <dcterms:issued>info:eu-repo/date/embargoEnd/2026-01-01</dcterms:issued>
   <dcterms:issued>info:eu-repo/date/embargoEnd/2026-01-01</dcterms:issued>
   <dcterms:issued>2016-10-14</dcterms:issued>
   <dc:type>info:eu-repo/semantics/article</dc:type>
   <dc:type>info:eu-repo/semantics/publishedVersion</dc:type>
   <dc:identifier>http://hdl.handle.net/10256/14108</dc:identifier>
   <dc:relation>info:eu-repo/semantics/altIdentifier/doi/10.1021/acscatal.6b01428</dc:relation>
   <dc:relation>info:eu-repo/semantics/altIdentifier/issn/2155-5435</dc:relation>
   <dc:relation>info:eu-repo/grantAgreement/MINECO//CTQ2014-59832-JIN/ES/ESCANEO COMPUTACIONAL DE RELACIONES ESTRUCTURA%2FACTIVIDAD DE CATALIZADORES DE OXIDACION DEL AGUA PARA LA GENERACION DE H2/</dc:relation>
   <dc:rights>Tots els drets reservats</dc:rights>
   <dc:rights>info:eu-repo/semantics/embargoedAccess</dc:rights>
   <dc:publisher>American Chemical Society (ACS)</dc:publisher>
   <dc:source>© ACS Catalysis, 2016, vol. 6, núm. 11, p. 7970–7976</dc:source>
   <dc:source>Articles publicats (D-Q)</dc:source>
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