1.
    发明专利
    未知

    公开(公告)号:DE4408950A1

    公开(公告)日:1995-09-21

    申请号:DE4408950

    申请日:1994-03-16

    Applicant: BASF AG

    Abstract: A process for producing aldehydes by the hydroformylation of olefins with more than 3 carbon atoms, comprising the hydroformylation stage by means of a rhodium catalyst uniformly dissolved in the reaction medium, the separation of the rhodium catalyst from the product from the hydroformylation reaction and its return to the hydroformylation stage, in which the rhodium catalyst is extracted into the aqueous phase by means of an aqueous solution of a nitrogen-containing complexing agent from the group of sulphonated pyridines, sulphonated quinolines, possibly substituted sulphonated or sulphonated component-containing 2,2' bipyridines, 1,10 phenanthrolines, 1,1' biquinolines, 2,2', 6', 2'' terpyridines and porphines, and/or from the group of carboxylated pyridines, carboxylated quinolines, possibly substituted, carboxylated or carboxylated substance-containing 2,2' bipyridines, 1,10 phenanthrolines, 2,2' biquinolines, 2,2', 6', 2'' terpyridines and porphines, and the alcohol and/or aldehyde is isolated and from the extracted hydroformylation product, the aqueous rodhium-containing extract is taken to a pre-carbonylation stage and subjected to a pre-carbonylation in said stage in the presence of a substantially water-soluble organic fluid and in the presence of carbon monoxide, synthesis gas or a carbon monoxide-containing gas mixture at a pressure of 50 to 100 bars and a temperature of 50 to 180 DEG C, the product from the pre-carbonylation stage is separated into an organic part containing the majority of the rhodium and an aqueous phase containing the complexing agents and the organic phase for the hydroformylation of the olefin is taken to the hydroformylation stage at 50 to 100 bars and a temperature of 50 to 180 DEG C.

    REACTOR FOR GAS/LIQUID OR GAS/LIQUID/SOLID REACTIONS

    公开(公告)号:MY138099A

    公开(公告)日:2009-04-30

    申请号:MYPI20021542

    申请日:2002-04-26

    Applicant: BASF AG

    Abstract: A REACTOR (1) HAVING A VERTICAL LONGITUDINAL AXIS AND AN INLET (2) FOR A LIQUID OR LIQUID/SOLID FEED STREAM IN THE UPPER REGION OF THE REACTOR AND AN INLET (3) FOR A GASEOUS STREAM IN THE LOWER REGION OF THE REACTOR (1), CHARACTERIZED BY - AT LEAST TWO CHAMBERS (4) ARRANGED ABOVE ONE ANOTHER IN THE LONGITUDINAL DIRECTION,WHERE - THE CHAMBERS (4) ARE SEPARATED FROM ONE ANOTHER BY LIQUID-TIGHT BOTTOM PLATES, - EACH CHAMBER IS CONNECTED VIA A LIQUID OVERFLOW (6) TO THE CHAMBER (4) LOCATEDIMMEDIATELY UNDERNEATH AND A LIQUID PRODUCT STREAM IS TAKEN OFF VIA THE LIQUID OVERFLOW (6) OF THE BOTTOMMOST CHAMBER (4), - THE GAS SPACE (7) ABOVE THE LIQUID SURFACE IN EACH CHAMBER (4) IS CONNECTED TO THECHAMBER (4) LOCATED IMMEDIATELY ABOVE IT BY ONE OR MORE GUIDE TUBES (8) WHICH OPENS (EACH OPEN) INTO A GAS DISTRIBUTOR (9) PROVIDED WITH OPENINGS FOR EXIT OF GASBELOW THE LIQUID SURFACE, - AND EACH CHAMBER IS PROVIDED WITH AT LEAST ONE GUIDE PLATE (12) WHICH IS ARRANGEDVERTICALLY AROUND EACH SIPHON LIKE GAS DISTRIBUTOR (9) AND WHOSE UPPER END IS BELOW THE LIQUID SURFACE AND WHOSE LOWER END IS ABOVE THE LIQUID - TIGHT BOTTOMPLATE (5) OF THE CHAMBER (4) AND WHICH DIVIDES EACH CHAMBER (4) INTO ONE OR MORESPACES INTO WHICH GAS FLOWS (13) AND ONE OR MORE SPACES INTO WHICH GAS DOESNOT FLOW (14), IS USED FOR GAS/LIQUID OR GAS/LIQUID/SOLID REACTIONS. (FIGURE 1)

    Static mixer for various substances

    公开(公告)号:DE19623105A1

    公开(公告)日:1997-12-11

    申请号:DE19623105

    申请日:1996-06-10

    Applicant: BASF AG

    Abstract: Static mixer with a helical mixing element formed from a strip which has been bent along its length to conform to the walls of the vessel, the bends being arranged particularly to run across the width of the strip. Also claimed is the method of using the mixer.

    Static mixer for fluids
    5.
    发明专利

    公开(公告)号:DE19623051A1

    公开(公告)日:1997-12-11

    申请号:DE19623051

    申请日:1996-06-10

    Applicant: BASF AG

    Abstract: A static mixer is claimed, in which the liquid components flow along sets of corrugated plates (3,3') so that flows from corresponding members of a set of plates meet at right angles, but in different planes. The plates extend partially over the internal diameter of the cylindrical mixing vessel (2). Also claimed is the process using this mixer.

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