2019
DOI: 10.1134/s2070050419040068
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Preparing High-Octane Motor Fuel Components via the Oxidation of an Industrial Isobutane Fraction

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“…The industrial liquid phase oxidation of isobutane with dioxygen is carried out below isobutane’s critical temperature ( T c = 135 °C), generating a mixture of TBA and TBHP. The TBHP is typically used as an oxidant for propylene epoxidation. To shift the selectivity toward TBA formation, there is interest in developing catalytic systems that can selectively decompose TBHP to TBA. ,− A variety of transition-metal based catalysts, such as Mn, , Ru, Fe, Cu, Eu, Co, and V, as well as halogenated metalloporphyrin complexes , have been reported for catalytic oxidation of various alkanes using dioxygen to produce oxygenated chemical precursors such as alcohols and acids.…”
Section: Introductionmentioning
confidence: 99%
“…The industrial liquid phase oxidation of isobutane with dioxygen is carried out below isobutane’s critical temperature ( T c = 135 °C), generating a mixture of TBA and TBHP. The TBHP is typically used as an oxidant for propylene epoxidation. To shift the selectivity toward TBA formation, there is interest in developing catalytic systems that can selectively decompose TBHP to TBA. ,− A variety of transition-metal based catalysts, such as Mn, , Ru, Fe, Cu, Eu, Co, and V, as well as halogenated metalloporphyrin complexes , have been reported for catalytic oxidation of various alkanes using dioxygen to produce oxygenated chemical precursors such as alcohols and acids.…”
Section: Introductionmentioning
confidence: 99%