21.
    发明专利
    未知

    公开(公告)号:DE19639520A1

    公开(公告)日:1998-04-09

    申请号:DE19639520

    申请日:1996-09-26

    Applicant: DEGUSSA

    Abstract: In an aluminium oxide (I) catalyst for the synthesis of methyl mercaptan containing 5-25 wt.% potassium tungstate (II) as promoter with respect to active (I), (II) is deposited in 2 portions. (I) is first coated with the first portion of (II) by impregnation in excess aqueous solution, then dried at elevated temperature. Then the second portion is applied by pore volume impregnation. The catalyst precursor is then dried at elevated temperature and calcined at 200-600 degrees C.

    25.
    发明专利
    未知

    公开(公告)号:DE19639520C2

    公开(公告)日:1998-10-01

    申请号:DE19639520

    申请日:1996-09-26

    Applicant: DEGUSSA

    Abstract: In an aluminium oxide (I) catalyst for the synthesis of methyl mercaptan containing 5-25 wt.% potassium tungstate (II) as promoter with respect to active (I), (II) is deposited in 2 portions. (I) is first coated with the first portion of (II) by impregnation in excess aqueous solution, then dried at elevated temperature. Then the second portion is applied by pore volume impregnation. The catalyst precursor is then dried at elevated temperature and calcined at 200-600 degrees C.

    PROCESS FOR THE EPOXIDATION OF OLEFINS.

    公开(公告)号:MY126269A

    公开(公告)日:2006-09-29

    申请号:MYPI20020313

    申请日:2002-01-28

    Abstract: THE INVENTION DESCRIBED HEREIN RELATES TO A PROCESS FOR THE CATALYTIC EPOXIDATION OF OLEFINS WITH HYDROGEN PEROXIDE IN A CONTINUOUS FLOW REACTION SYSTEM. WHEREIN THE REACTION MIXTURE IS PASSED THROUGH A FIXED CATALYST BED WITHIN A REACTOR EQUIPPED WITH COOLING MEANS WHILE MAINTAINING A TEMPERATURE PROFILE WITHIN THE REACTOR SUCH THAT THE COOLING MEDIUM TEMPERATURE OF THE COOLING MEANS IS AT LEAST 40°C AND THE MAXIMUM TEMPERATURE WITHIN THE CATALYST BED IS 60°C AT THE MOST.

    30.
    发明专利
    未知

    公开(公告)号:DE19617040C1

    公开(公告)日:1997-10-30

    申请号:DE19617040

    申请日:1996-04-27

    Applicant: DEGUSSA

    Abstract: Production of catalytically active coatings on the surface of ceramic mouldings comprises uniformly wetting the mouldings with a coating dispersion containing a particulate Pt metal and a further coating component in a carrier fluid, vaporising the carrier fluid, and converting the coating into the catalytically active state by slowing heating in the presence of nitrogen and/or ammonia to 1000-1350 degrees C. Particulate nitrides with Al, B, Ti or Si as cations are used as the further component. The particulate components have an average particle size of

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