Energy & Environmental Science · 2010 · 129 citations · 35 references
Natural SciencesChemical EngineeringChemistryCatalysisInorganic ChemistryReaction EngineeringCatalytic MaterialsCatalytic Reaction EngineeringCatalytic Reaction KineticsHeterogeneous CatalysisIndustrial CatalysisSupported CatalystsAlternative Diesel FuelsAlternative FuelsAromatic HydrocarbonsCatalytic Process OptimizationCation ExchangeFractional DistillationIsomerization ProcessesRenewable Feedstock Conversion
An efficient method for the selective dimerization of the renewable feedstock, 2-ethyl-1-hexene, to a complex mixture of C16H32 hydrocarbons has been developed. To optimize the process, the activity of a variety of strongly acidic heterogeneous catalysts was investigated. Montmorillonite K-10 and sulfated zirconia readily isomerized 2-ethyl-1-hexene to a mixture of the cis- and trans isomers of 3-methyl-2-heptene and 3-methyl-3-heptene, but were inactive for the dimerization of 2-ethyl-1-hexene at temperatures up to 116 °C. In contrast, the cation exchange resins Amberlyst-15 and Nafion, readily dimerized 2-ethyl-1-hexene at elevated temperatures. For both sets of catalysts, the degree of hydration strongly affected the rate of isomerization/dimerization. After hydrogenation over PtO2 and fractional distillation, saturated dimer mixtures could be isolated in up to 90% yield. The dimers have a density of 0.78 g mL−1 and a freezing point <−60 °C, suggesting that they can be blended with renewable or conventional jet fuels, without adversely affecting the overall density and low temperature viscosity of the mixtures.
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Solid acid catalysis using ion-exchange resins
Mark A. Harmer, Qun Sun · Applied Catalysis A General · 2001 · 633 citations