1.
    发明专利
    未知

    公开(公告)号:DE2613352A1

    公开(公告)日:1977-10-06

    申请号:DE2613352

    申请日:1976-03-29

    Applicant: BASF AG

    Abstract: A process for the manufacture of high impact and translucent polystyrene, in which, in a first stage, styrene is prepolymerized in mass or in solution in the presence of a rubber, and the polymerization is then completed in mass, in solution or in aqueous suspension. The prepolymerization is taken to a stage where the amount of styrene converted is from 3 to 10 times the amount of the elastomer constituent of the rubber, and at this conversion the disperse soft-component phase formed should have a mean particle size of less than 1 mu m and should contain from 35 to 65% by weight of free or chemically bonded polystyrene segments. The translucent styrene polymers of high impact strength may be used for packaging purposes.

    2.
    发明专利
    未知

    公开(公告)号:DE3044118A1

    公开(公告)日:1982-06-24

    申请号:DE3044118

    申请日:1980-11-24

    Applicant: BASF AG

    Abstract: Polyacetal molding materials which contain, as a stabilizer, from 0.1 to 10% by weight of a melamine resin, the latter being a melamine-formaldehyde condensate, having a mean degree of polymerization of from 1.2 to 6.0 and a melamine:formaldehyde ratio of from 1:2 to 1:5.5, which has been partially etherified with a C1-C4-alkanol so that the ratio melamine:ether radicals is from 1:1.5 to 1:5.0 and the ratio melamine:free methylol groups is from 1:0.5 to 1:3. The molding materials can be converted to moldings which can be used industrially at elevated ambient temperatures.

    Process for the continuous bulk polymerisation of trioxane

    公开(公告)号:DE3207773A1

    公开(公告)日:1982-09-16

    申请号:DE3207773

    申请日:1982-03-04

    Applicant: BASF AG

    Abstract: The invention relates to a process for the continuous bulk polymerisation of trioxane with the aid of cationic polymerisation initiators in a plurality of zones: in the first polymerisation zone A, liquid trioxane is polymerised to a conversion of from 30 to 80% at a pressure of from 2 to 100 bar and at a temperature at the exit to the zone of from 116 to 160 DEG C; in a decompression zone B, the resultant suspension is decompressed to atmospheric pressure, during which from 10 to 60% of the trioxane originally employed evaporates; in a second polymerisation zone C, the polymerisation is continued at a temperature of from 65 to 115 DEG C.

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