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    • 3. 发明申请
    • PROCESS FOR PREPARING AN EPOXIDATION CATALYST
    • WO2021038027A1
    • 2021-03-04
    • PCT/EP2020/074057
    • 2020-08-28
    • BASF SE
    • KARPOV, AndreyRUETTINGER, WolfgangWALSDORFF, ChristianBARTOSCH, ChristianGROBYS, Mauricio
    • B01J21/04B01J23/50B01J23/68B01J35/00B01J35/02B01J35/04B01J35/10B01J37/00B01J37/02
    • A process for preparing a catalyst for producing ethylene oxide by gas-phase oxidation of ethylene comprises i) impregnating a porous alumina support having a packed tube density in the range of 100 to 450 g/L; a Log differential pore volume distribution curve, 5 as measured by mercury porosimetry, having at least one peak in a pore diameter range of 0.01 to 5.0 µm; and a BET surface area in the range of 1.5 to 30.0 m2/g; with a silver impregnation solution, preferably under reduced pressure; and optionally subjecting the impregnated porous alumina support to drying; and ii) subjecting the impregnated porous alumina support to a calcination process; wherein steps i) and ii) are optionally repeated, 10 to yield a catalyst comprising at least 25 wt.-% of silver, relative to the total weight of the catalyst. The catalyst shows high activity and selectivity. The invention further relates to a catalyst for producing ethylene oxide by gas-phase oxidation of ethylene, obtainable by a process as defined above. The invention also relates to a catalyst for producing ethylene oxide by gas-phase oxidation of ethylene, comprising at least 25 wt.-% of silver, 15 relative to the total weight of the catalyst, deposited on a porous alumina support, the support having i) a packed tube density in the range of 100 to 450 g/L, preferably 150 to 450 g/L, more preferably 200 to 400 g/L; ii) a Log differential pore volume distribution curve, as measured by mercury porosimetry, having at least one peak in a pore diameter range of 0.01 to 5.0 µm; and iii) a BET surface area in the range of 1.5 to 30.0 m2/g, 20 preferably 1.5 to 20.0 m2/g, more preferably 2.0 to 10.0 m2/g, most preferably 2.5 to 8.0 m2/g, in particular 3.0 to 7.0 m2/g. The invention further relates to a process for producing ethylene oxide by gas-phase oxidation of ethylene, comprising reacting ethylene and oxygen in the presence of a catalyst as defined above.