PREPARATION OF MALEIC ANHYDRIDE
    13.
    发明专利

    公开(公告)号:MY136413A

    公开(公告)日:2008-09-30

    申请号:MYPI20042577

    申请日:2004-06-29

    Applicant: BASF AG

    Abstract: A PROCESS FOR PREPARING MALEIC ANHYDRIDE BY OXIDIZING n-BUTANE IN THE GAS PHASE UNDER HETEROGENEOUS CATALYSIS WITH OXYGEN-CONTAINING GASES OVER A VANADIUM-, PHOSPHORUS-AND OXYGEN-CONTAINING CATALYST IN A REACTOR UNIT AT A TEMPERATURE IN THE RANGE FROM 350 TO 500°C, REMOVING THE MALEIC ANHYDRIDE FORMED TO FORM A GAS STREAM WHICH COMPRISES UNCONVERTED n-BUTANE AND WATER AND RECYCLING AT LEAST A PORTION OF THE UNCONVERTED n-BUTANE TO THE REACTOR UNIT, BY FEEDING TO THE REACTOR UNIT AN INLET STREAM HAVING AN n-BUTANE CONCENTRATION OF FROM 0.5 TO 1.5BY VOLUME AND AN OXYGEN CONCENTRATION OF FROM 5 TO 21BY VOLUME, ESTABLISHING A PRESSURE AT THE INLET TO THE REACTOR UNIT OF FORM 0.4 TO 2 MPa ABS, AND CONVERTING FORM 40 TO 100OF THE n-BUTANE FROM THE INLET STREAM PER REACTOR PASS.

    14.
    发明专利
    未知

    公开(公告)号:DE502006000261D1

    公开(公告)日:2008-02-14

    申请号:DE502006000261

    申请日:2006-06-30

    Applicant: BASF AG

    Abstract: The invention relates to a process for separating off maleic anhydride from a gas stream comprising maleic anhydride, in which a) the gas stream comprising maleic anhydride is brought into contact with a liquid absorbent phase comprising at least one high-boiling inert absorption medium for maleic anhydride and b) maleic anhydride is separated off from the resulting liquid absorbate phase by stripping with a hydrogen-comprising gas as stripping medium in a column, wherein the stripping medium is fed in at two points on the column which are at least one theoretical plate apart.

    20.
    发明专利
    未知

    公开(公告)号:DE102005004604A1

    公开(公告)日:2006-08-10

    申请号:DE102005004604

    申请日:2005-02-01

    Applicant: BASF AG

    Abstract: The invention relates to a method of controlling a hydrogenation of a starting material in a hydrogenation reactor, in which the amount of hydrogen reacted in the hydrogenation is firstly determined, the ratio of the amount of hydrogen reacted to the amount of starting material fed in is then derived, this ratio is compared with a prescribed value and, finally, at least one process parameter is altered if the ratio of the amount of hydrogen reacted to the amount of starting material fed in deviates by a prescribed amount from the prescribed value.

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