Direct Gas-Phase Epoxidation of Propene with Hydrogen Peroxide on TS-1 Zeolite in a Microstructured Reactor
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文摘
Direct epoxidation of propene with hydrogen peroxide vapor was conducted in a microstructured reactorcontaining TS-1 catalyst coatings. At 140 C, 1 bar, 5 vol % hydrogen peroxide, and 15 vol % propene,productivities of more than 1 kg of propene oxide per kg of catalyst and hour are obtained in lab scale, whichis in an industrially highly relevant range. Excellent selectivities to propene oxide based on propene of >90%were reached. Potential and need for improvement lie in the propylene oxide selectivity based on hydrogenperoxide, which was observed to be about 25%. By increasing the molar excess of propene to about 6.6,propylene oxide selectivities related to hydrogen peroxide of up to 60% have been observed in the pilotplant.

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