71.
    发明专利
    未知

    公开(公告)号:AT269285T

    公开(公告)日:2004-07-15

    申请号:AT01927780

    申请日:2001-03-22

    Applicant: BASF AG

    Abstract: A process for the production of essentially unsaturated oligomers of 4-6C alkenes from an alkene or alkene containing hydrocarbon stream at a nickel containing heterogeneous catalyst in an adiabatic reactor at 20-300 [deg]C and 1-100 bar comprises working up a first partial outlet stream to the oligomer and recycling a second partial stream together with fresh alkene to the reactor.

    73.
    发明专利
    未知

    公开(公告)号:AT238838T

    公开(公告)日:2003-05-15

    申请号:AT99944416

    申请日:1999-08-17

    Applicant: BASF AG

    Abstract: A coated catalyst for the catalytic gas-phase oxidation of aromatic hydrocarbons comprises, on an inert nonporous support, a catalytically active composition comprising a defined amount of vanadium oxide, titanium dioxide, a cesium compound, a phosphorus compound, and antimony oxide, wherein the catalytically active composition is applied in two or more layers and where relative to the inner layer or inner layers the outer layer has an antimony oxide content which is from 50 to 100% lower and wherein the amount of catalytically active composition of the inner layer or layers is from 10 to 90% by weight of the amount of catalytically active composition, and can be used for preparing carboxylic acids and/or anhydrides, in particular phthalic anhydride; also specified is a production process for such catalysts.

    76.
    发明专利
    未知

    公开(公告)号:DE10040827A1

    公开(公告)日:2002-03-07

    申请号:DE10040827

    申请日:2000-08-21

    Applicant: BASF AG

    Abstract: The invention relates to a method for producing phthalic anhydride by the gas phase oxidation of xylene, naphthalene or mixtures thereof in a multitube fixed-bed reactor, which is thermostatted by a heat-transfer medium, on two different fixed-bed catalysts arranged in layers. The invention method is carried out in such a manner that the maximum temperature in the second catalyst layer arranged in the direction of flow is approximately at least 52 DEG C lower than the maximum temperature in the first catalyst layer. The inventive method enables the production of phthalic anhydride with high yields under conditions relevant to practice.

    Method for the vapour-phase partial oxidation of aromatic hydrocarbons

    公开(公告)号:AU9177901A

    公开(公告)日:2002-03-04

    申请号:AU9177901

    申请日:2001-08-20

    Applicant: BASF AG

    Abstract: Aromatic hydrocarbons are partially oxidized in the gas phase over a catalyst at elevated temperature to form carboxylic acids or carboxylic anhydrides in a process in which a gas stream laden with the starting materials is passed through a shell-and-tube reactor whose temperature is controlled by means of one or more separate thermostatting baths conveyed in countercurrent to the starting gas stream, wherein the difference between the temperature of the thermostatting bath in the region of the reactor outlet and the temperature of the product gas stream leaving the reactor is employed to control the selectivity of the gas-phase oxidation.

    Method for producing phthalic anhydride

    公开(公告)号:AU1214402A

    公开(公告)日:2002-03-04

    申请号:AU1214402

    申请日:2001-08-20

    Applicant: BASF AG

    Abstract: A process for preparing phthalic anhydride by gas-phase oxidation of xylene, naphthalene or mixtures thereof over two different fixed-bed catalysts arranged in zones in a shell-and-tube reactor which is thermostated by means of a heat transfer medium is carried out so that the maximum temperature in the second catalyst zone in the flow direction is at least 52° C. lower than the maximum temperature in the first catalyst zone.The process of the present invention makes it possible to prepare phthalic anhydride in high yields under conditions relevant to industrial practice.

    79.
    发明专利
    未知

    公开(公告)号:DE10026906A1

    公开(公告)日:2001-12-06

    申请号:DE10026906

    申请日:2000-05-31

    Applicant: BASF AG

    Abstract: The invention relates to a method for shutting down a reactor used to oligomerize alkenes on a heterogeneous catalyst containing nickel. According to the inventive method, the amount of alkenes in the feed stream to the reactor is decreased by using a hydrocarbon flow which is substantially devoid of aromatic compounds. The amount of alkenes in the feed stream to the reactor is reduced to less than 10 % wt. % of the total feed stream so that the temperature of the catalyst does not exceed or does not substantially exceed the maximum temperature of the catalyst in a productive operational mode before the shut down occurs. The hydrocarbon flow which is substantially devoid of aromatic compounds and which is used partially or fully is the flow which is retained when the oligomer products are separated from the reactor discharge.

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