Industrial & Engineering Chemistry Research · 2010 · 21 citations · 28 references
Materials ScienceChemical EngineeringMethyl Isobutyl KetoneEngineeringEnantioselective SynthesisCatalytic ProcessOrganic ChemistryCatalysisChemistryHydrogenGas Phase ProductionHigh SelectivitySynthesis MethodCatalyst PreparationCatalyst ActivationCatalytic Synthesis
In this paper, we have examined the activity and selectivity of catalysts for the one-step, gas phase production of methyl isobutyl ketone (MIBK) from acetone (propanone) over the temperature range 373−573 K. The catalysts used were an impregnated MgO/silica, a Pd-MgO/silica formed from coimpregnation of the nitrates, and a Pd supported on a 1% Mg doped silica, Pd/Mg-SiO2. Using MgO/silica, mesityl oxide (MO) was formed with 100% selectivity at 373 and 473 K. Addition of Pd gave 100% selectivity to MIBK at 373 K, albeit at low conversion. Pd-MgO/silica revealed a promotional effect of the MgO on the hydrogenation function of the Pd and a promotional effect of the Pd on the aldol condensation activity of the MgO. The Pd/Mg-SiO2 catalyst showed high selectivity but low conversion, as no promoting effect was observed.
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