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    Catalyst for the production of maleic anhydride
    2.
    发明专利
    Catalyst for the production of maleic anhydride 未知

    公开(公告)号：GB1141343A

    公开(公告)日：1969-01-29

    申请号：GB950566

    申请日：1966-03-04

    Applicant: BASF AG

    Inventor： FRIEDRICHSEN WILHELM ,  STEPHAN HANS JOACHIM

    IPC: B01J23/30 ,  B01J27/186 ,  B01J27/199 ,  C07C51/25 ,  C07C51/31

    Abstract: 1,141,343. Maleic anhydride. BADISCHE ANILIN- & SODA-FABRIK A.G. 4 March, 1966 [5 March, 1965], No. 9505/66. Heading C2C. [Also in Division B1] Benzene or olefinically unsaturated aliphatic hydrocarbons having 4C e.g. butene - 1 or -2 or butadiene are oxidized to maleic anhydride in the presence of a catalyst containing 1-80% V 2 O 5 , 1-40% WO 3 , 0À5-35% P 2 0 5 and 10- 95% TiO 2 the latter serving as catalyst carrier for the other components. The feed hydrocarbon may contain other hydrocarbons e.g. butane or 5 or 6 C saturated or unsaturated. Oxidation is preferably effected using a mixture of oxygen and nitrogen e.g. at 300-500‹ C. In Examples 1-3 benzene is oxidized to maleic anhydride and in Example 4 a gaseous mixture containing butenes-1 and -2, butane and isobutylene is similarly oxidized.

    Production of pure maleic anhydride
    5.
    发明专利
    Production of pure maleic anhydride 未知

    公开(公告)号：GB946724A

    公开(公告)日：1964-01-15

    申请号：GB853562

    申请日：1962-03-06

    Applicant: BASF AG

    Inventor： FRIEDRICHSEN WILHELM ,  STEPHAN HANS JOACHIM

    Abstract: Maleic anhydride, 99.7 to 99.8% pure and free from fumaric acid, is produced by introducing maleic acid, or an aqueous solution or suspension containing at least 50% by weight thereof, into maleic anhydride boiling at atmospheric or reduced pressure thereby vaporizing maleic anhydride and water; cooling the vapours by 3 to 30 DEG C., preferably 5 to 20 DEG C., but not below 100 DEG C., in a first condensation zone; removing the condensed maleic anhydride; cooling the remaining vapours to 30 DEG to 80 DEG C. below that of the first condensation zone, but not below the dew point of water vapour at the prevailing pressure and not below 53 DEG C.; returning the condensate to the vaporizing mixture and condensing the water vapour leaving the second condensation zone. In a specific embodiment maleic acid, or an aqueous solution or suspension thereof, is passed from vessel 1 into vaporizer 2 which contains boiling maleic anhydride at 110 DEG to 200 DEG C. and 50 to 760 mm.Hg., being preferably 115 DEG to 140 DEG C. at 90 to 150 mm. Hg. It is convenient to maintain an amount of anhydride, advantageously 70 to 95% by weight of the contents of the vessel, in 2 such that the mixture remains homogeneously liquid and to introduce the maleic acid into 2.3 to 17 times its own weight of anhydride. The vapours are passed through column 3, maintained at the same temperature as 2, into the first condensation zone 4, where they are cooled by 3 to 30 DEG C. to condense part of the anhydride (approx. 15 to 35%) contained therein, which is collected in pure form in vessel 5. The remaining vapours are cooled in the second condensation zone (6) to such a temperature that the bulk of anyhdride is separated in lquid form but the water vapour remains substantially uncondensed. The condensate from 6 is passed via pipe 7 and column 3 to the vaporizing mixture in 2 and the residual vapours are condensed in column 8, collected in vessel 9 and may be used for washing maleic anhydride gases from the combustion products of benzene. The ratio between maleic anhydride condensed in the first zone to that in the second, controlled by the temperature of the two zones, is 1:6 to 1:1. Examples are given.

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