FUNKTIONALISIERTE POLYOXYMETHYLEN-BLOCK-COPOLYMERE
    3.
    发明公开
    FUNKTIONALISIERTE POLYOXYMETHYLEN-BLOCK-COPOLYMERE 有权
    FUNKTIONALISIERTE聚氧乙烯嵌段共聚物

    公开(公告)号:EP2935381A2

    公开(公告)日:2015-10-28

    申请号:EP13814099.1

    申请日:2013-12-18

    摘要: The invention relates to a method for producing functionalized polyoxymethylene block copolymers comprising the step of polymerizing formaldehyde in a reaction vessel in the presence of a catalyst, the polymerization of formaldehyde in addition taking place in the presence of a starter compound comprising at least 2 Zerewitinoff active H atoms, to obtain an intermediate product. The intermediate product obtained is subsequently reacted with a cyclic carboxylic acid ester or carbonic acid ester, thus obtaining a functionalized polyoxymethylene block copolymer. The invention further relates to functionalized polyoxymethylene block copolymers obtained by such a method and to the use of said copolymers.

    摘要翻译: 本发明涉及一种生产官能化聚甲醛嵌段共聚物的方法,其包括在催化剂存在下在反应容器中聚合甲醛的步骤,另外在存在起始化合物的情况下进行甲醛的聚合,所述起始化合物包含至少2个Zerewitinoff活性 H原子,得到中间产物。 随后将所得中间产物与环状羧酸酯或碳酸酯反应,得到官能化聚甲醛嵌段共聚物。 本发明还涉及通过这种方法获得的官能化聚甲醛嵌段共聚物和所述共聚物的用途。

    PROCESS FOR PRODUCTION OF PERFLUOROPOLYETHER CARBOXYLIC ACID FLUORIDE
    10.
    发明公开
    PROCESS FOR PRODUCTION OF PERFLUOROPOLYETHER CARBOXYLIC ACID FLUORIDE 有权
    用于生产全氟聚醚CARBOXYLSÄUREFLUORID

    公开(公告)号:EP1980584A1

    公开(公告)日:2008-10-15

    申请号:EP07707881.4

    申请日:2007-02-01

    发明人: IKEDA, Sunao

    IPC分类号: C08G65/323 C08G65/16

    摘要: Perfluoropolyether carboxylic acid fluoride having the following general formula :

            F(CF 2 CF 2 CF 2 O)nCF 2 CF 2 COF

    (n : 2-200, preferably 35-70)
    can be produced by starting fluorination reaction of polyfluoropolyether carboxylic acid having the general formula as a tetrafluorooxetane polymer :

            F(CH 2 CF 2 CF 2 O)nCH 3 CF 2 COF

    (n: 2-200)
    in a dispersed state in a perfluoropolyether-based solvent with a fluorine gas at 50 ° -80 °C, then slowly elevating the fluorination reaction temperature, and finally completing the fluorination reaction at 100° - 120°C, where even in the case of fluorination reaction of the starting material with a high degree of polymerization the desired product can be produced in high yield, while suppressing the decomposition and keeping the high degree of polymerization substantially.