PRODUCTION METHOD OF OLEFIN POLYMER AND OLEFIN POLYMERIZATION CATALYST
    2.
    发明申请
    PRODUCTION METHOD OF OLEFIN POLYMER AND OLEFIN POLYMERIZATION CATALYST 有权
    烯烃聚合物和烯烃聚合催化剂的生产方法

    公开(公告)号:US20160039952A1

    公开(公告)日:2016-02-11

    申请号:US14773638

    申请日:2014-03-11

    Abstract: To provide a method of efficiently affording olefin polymers having a high molecular weight and a high melting point even under industrially advantageous high-temperature conditions. A production method of an olefin polymer to solve the above problem includes polymerizing monomer(s) including at least one α-olefin having 3 or more carbon atoms at 50° C. to 200° C. in the presence of an olefin polymerization catalyst including; (A) a crosslinked metallocene compound represented by General Formula [I] below; and (B) at least one compound selected from (b-1) an organoaluminum oxy-compound, (b-2) a compound that forms an ion pair by reacting with the crosslinked metallocene compound (A), and (b-3) an organoalunimum compound.

    Abstract translation: 提供即使在工业上有利的高温条件下也能有效地提供具有高分子量和高熔点的烯烃聚合物的方法。 为了解决上述问题,烯烃聚合物的制造方法包括在烯烃聚合催化剂的存在下,在50℃〜200℃下聚合包含至少一种碳原子数3以上的α-烯烃的单体,所述烯烃聚合催化剂包括 ; (A)下述通式[I]表示的交联金属茂化合物; 和(B)至少一种选自(b-1)有机铝氧化合物的化合物,(b-2)通过与交联的茂金属化合物(A)反应形成离子对的化合物和(b-3) 有机最合物。

    LUBRICATING OIL COMPOSITION
    3.
    发明申请

    公开(公告)号:US20220275304A1

    公开(公告)日:2022-09-01

    申请号:US17636823

    申请日:2020-08-26

    Abstract: A lubricating oil composition with a resin (A) and a base oil (B), the resin (A) is in a range of 0.01 to 50 parts by mass per 100 parts of (A) and (B), the resin (A) satisfies the following requirements: (A-1) the resin (A) is a polymer including a constituent unit from 4-methyl-1-pentene in a range of 60 to 99 mol % and a constituent unit from an α-olefin having 2 to 20 carbon atoms (excluding 4-methyl-1-pentene) in a range of 1 to 40 mol % (provided that 4-methyl-1-pentene and the α-olefin is 100 mol %); (A-2) intrinsic viscosity [η] measured in decalin at 135° C. is in a range of 0.01 to 5.0 dl/g; (A-3) a melting point (Tm) is in a range of 110 to 150° C. as determined by DSC; and the base oil (B) has (B-1) kinematic viscosity at 100° C. is in a range of 1 to 50 mm2/s.

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