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   <dc:title>Ion exchange resins as catalysts for the liquid-phase dehydration of 1-butanol to di-n-butyl ether</dc:title>
   <dc:creator>Pérez-Maciá, María Ángeles</dc:creator>
   <dc:creator>Bringué Tomàs, Roger</dc:creator>
   <dc:creator>Iborra Urios, Montserrat</dc:creator>
   <dc:creator>Tejero Salvador, Xavier</dc:creator>
   <dc:creator>Cunill García, Fidel</dc:creator>
   <dc:subject>Èters</dc:subject>
   <dc:subject>Resines de bescanvi iònic</dc:subject>
   <dc:subject>Catàlisi</dc:subject>
   <dc:subject>Alcohol butílic</dc:subject>
   <dc:subject>Ethers</dc:subject>
   <dc:subject>Ion exchange resins</dc:subject>
   <dc:subject>Catalysis</dc:subject>
   <dc:subject>Butanol</dc:subject>
   <dc:description>This work reports the production of di-n-butyl ether (DNBE) by means of 1-butanol dehydration in the liquid phase on acidic ion-exchange resins. Dehydration experiments were performed at 150 ºC and 40 bar on 13 styrene-codivinylbenzene ion exchangers of different morphology. By comparing 1-butanol conversions to DNBE and initial reaction rates it is concluded that oversulfonated resins are the most active catalysts for 1-butanol dehydration reaction whereas gel-type resins that swell significantly in the reaction medium as well as the macroreticular thermostable resin Amberlyst-70 are the most selective to DNBE. The highest DNBE yield was achieved on Amberlyst 36. The influence of typical 1-butanol impurities on the dehydration reaction were also investigated showing that the presence of 2-methyl-1-propanol (isobutanol) enhances the formation of branched ethers such as 1-(1-methylpropoxy) butane and 1-(2-methylpropoxy) butane, whereas the presence of ethanol and acetone yields ethyl butyl ether and, to a much lesser extent, diethyl ether.</dc:description>
   <dc:date>2016-05-31T11:40:26Z</dc:date>
   <dc:date>2016-05-31T11:40:26Z</dc:date>
   <dc:date>2014-05-24</dc:date>
   <dc:date>2016-05-31T11:40:31Z</dc:date>
   <dc:type>info:eu-repo/semantics/article</dc:type>
   <dc:type>info:eu-repo/semantics/acceptedVersion</dc:type>
   <dc:identifier>0926-860X</dc:identifier>
   <dc:identifier>https://hdl.handle.net/2445/99085</dc:identifier>
   <dc:identifier>641825</dc:identifier>
   <dc:language>eng</dc:language>
   <dc:relation>Versió postprint del document publicat a: http://dx.doi.org/10.1016/j.apcata.2014.05.017</dc:relation>
   <dc:relation>Applied Catalysis A-General, 2014, vol. 482, p. 38-48</dc:relation>
   <dc:relation>http://dx.doi.org/10.1016/j.apcata.2014.05.017</dc:relation>
   <dc:rights>(c) Elsevier B.V., 2014</dc:rights>
   <dc:rights>info:eu-repo/semantics/openAccess</dc:rights>
   <dc:format>11 p.</dc:format>
   <dc:format>application/pdf</dc:format>
   <dc:publisher>Elsevier B.V.</dc:publisher>
   <dc:source>Articles publicats en revistes  (Enginyeria Química i Química Analítica)</dc:source>
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