Manufacture of aliphatic fluorine componds

    公开(公告)号:GB863545A

    公开(公告)日:1961-03-22

    申请号:GB3357057

    申请日:1957-10-28

    Applicant: HOECHST AG

    Abstract: Aliphatic fluorine compounds are obtained by reacting vaporous hydrogen fluoride with the vapour of a halogenated aliphatic hydrocarbon containing one or more halogen atoms (other than fluorine) and which may additionally contain one or more fluorine atoms, the reaction being carried out in the presence of a catalyst comprising aluminium fluoride and at a temperature in the range of 200 DEG -300 DEG C. In an example, a nickel tube is filled with pieces of porous alumina impregnated with magnesium chloride; and a current of gaseous hydrogen fluoride is passed through the tube for 20 hours at 200 DEG -250 DEG C. A mixture of the vapours of carbon tetrachloride (1 mol per hour) and hydrogen fluoride (1.86 mols per hour) is then passed through the tube at 230 DEG -250 DEG C. The reaction product consisted of difluorodichloromethane and monofluorotrichloromethane, together with a minor proportion of trifluoromonoschloromethane. Specification 805,503 also is referred to.

    13.
    发明专利
    未知

    公开(公告)号:NO943647L

    公开(公告)日:1994-09-30

    申请号:NO943647

    申请日:1994-09-30

    Applicant: HOECHST AG

    Abstract: PCT No. PCT/EP93/00675 Sec. 371 Date Sep. 30, 1994 Sec. 102(e) Date Sep. 30, 1994 PCT Filed Mar. 19, 1993 PCT Pub. No. WO93/20255 PCT Pub. Date Oct. 14, 1993The invention relates to a process for producing a strong bond between copper layers, which have been applied by means of thermal spraying of pulverulent copper or copper alloys, and ceramic. Fine copper powder having a mean particle diameter of

    Process and device for the manufacture of trifluorobromomethane

    公开(公告)号:GB949877A

    公开(公告)日:1964-02-19

    申请号:GB4290061

    申请日:1961-11-30

    Applicant: HOECHST AG

    Abstract: Trifluorobromomethane is produced in a continuous process wherein chloroform is fluorinated with an excess of gaseous hydrogen fluoride and the trifluoromethane so formed is brominated, after the removal of hydrogen chloride and hydrogen fluoride therefrom, using an excess of bromine in a reaction vessel the walls of which have an inner surface consisting of a sintered oxide of a metal of Group II to IV of the Periodic Table. It is of advantage to use up to a 50% mole excess of hydrogen fluoride and of bromine with a fluorination temperature of at least 300 DEG C., preferably 420 DEG to 500 DEG C. and a bromination temperature of 650 DEG to 800 DEG C., preferably 700 DEG to 750 DEG C.Suitable oxides mentioned are aluminium, zirconium and magnesium oxides. An aluminium fluoride catalyst may be used in the fluorination process. Specification 770,640 is referred to.ALSO:Trifluoromethane is brominated in a reaction zone bounded by walls of which the inner surfaces consist of a sintered oxide of a metal of Group II to IV of the Periodic Table. The reaction zone may take the form of tubes, provided with external heating means, made from the sintered oxide, preferably aluminium oxide, and being connected together by metal couplings which are not heated and which consist of special steels or alloys thereof, or preferably consist of nickel. Other oxides mentioned are zirconium and magnesium oxides. Specification 770,640 is referred to.

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