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    • 1. 发明授权
    • Polymerisation process
    • 聚合过程
    • US07705095B2
    • 2010-04-27
    • US10583115
    • 2004-12-08
    • Brian Stephen KimberleyGerard LacaneSergio Mastroianni
    • Brian Stephen KimberleyGerard LacaneSergio Mastroianni
    • C08F4/64C08F4/52C08F2/00
    • C08F210/16C08F4/65908C08F4/65916C08F4/6592Y10S526/901C08F2/005C08F4/65912C08F210/14C08F2500/24
    • A process for the polymerisation of olefin monomers selected from (a) ethylene, (b) propylene (c) mixtures of ethylene and propylene and (d) mixtures of (a), (b) or (c) with one or more other alpha-olefins is performed in a polymerisation reactor in the presence of a supported polymerisation catalyst characterised in that prior to injection into the reactor said supported polymerisation catalyst in the form of a powder is contacted with an inert hydrocarbon liquid in a quantity sufficient to maintain said catalyst in powder form. The preferred inert hydrocarbon liquid is hexane. The supported polymerisation catalyst is preferably a supported metallocene catalyst. According to the process of the prescrit invention the level of fines associated with the polymer products is reduced in particular the level of fines having a diameter
    • 聚合烯烃单体的方法,其选自(a)乙烯,(b)丙烯(c)乙烯和丙烯的混合物和(d)(a),(b)或(c)的混合物与一种或多种其它α 烯烃在聚合反应器中在负载的聚合催化剂存在下进行,其特征在于在注入反应器之前,将所述粉末形式的所述载体聚合催化剂与足以维持所述催化剂的量的惰性烃液体接触 以粉末形式。 优选的惰性烃液体是己烷。 负载型聚合催化剂优选为负载金属茂催化剂。 根据预发明的方法,与聚合物产物相关的细粒水平特别降低了直径<125μm的细粒和直径<50μm的微细粒子的水平。
    • 2. 发明申请
    • Polymerisation process
    • 聚合过程
    • US20070066773A1
    • 2007-03-22
    • US10583115
    • 2004-12-08
    • Brian KimberleyGerard LacaneSergio Mastroianni
    • Brian KimberleyGerard LacaneSergio Mastroianni
    • C08F4/44
    • C08F210/16C08F4/65908C08F4/65916C08F4/6592Y10S526/901C08F2/005C08F4/65912C08F210/14C08F2500/24
    • A process for the polymerisation of olefin monomers selected from (a) ethylene, (b) propylene (c) mixtures of ethylene and propylene and (d) mixtures of (a), (b) or (c) with one or more other alpha-olefins is performed in a polymerisation reactor in the presence of a supported polymerisation catalyst characterised in that prior to injection into the reactor said supported polymerisation catalyst in the form of a powder is contacted with an inert hydrocarbon liquid in a quantity sufficient to maintain said catalyst in powder form. The preferred inert hydrocarbon liquid is hexane. The supported polymerisation catalyst is preferably a supported metallocene catalyst. According to the process of the prescrit invention the level of fines associated with the polymer products is reduced in particular the level of fines having a diameter
    • 聚合烯烃单体的方法,其选自(a)乙烯,(b)丙烯(c)乙烯和丙烯的混合物和(d)(a),(b)或(c)的混合物与一种或多种其它α 烯烃在聚合反应器中在负载的聚合催化剂存在下进行,其特征在于在注入反应器之前,将所述粉末形式的所述载体聚合催化剂与足以维持所述催化剂的量的惰性烃液体接触 以粉末形式。 优选的惰性烃液体是己烷。 负载型聚合催化剂优选为负载金属茂催化剂。 根据预制发明的方法,与聚合物产物相关的细粒水平特别降低了直径<125μm的细粒和直径<50μm的微细粒子的水平。