PRODUCING POLYOLEFIN PRODUCTS
    1.
    发明公开

    公开(公告)号:EP4198064A1

    公开(公告)日:2023-06-21

    申请号:EP23155448.6

    申请日:2015-02-10

    Abstract: Catalyst systems and methods for making and using the same. A method of polymerizing olefins to produce a polyolefin polymer with a multimodal composition distribution, includes contacting ethylene and a comonomer with a catalyst system. The catalyst system includes a first catalyst compound and a second catalyst compound that are co-supported to form a commonly supported catalyst system. The first catalyst compound includes a compound with the general formula (C 5 H a R 1 b )(C 5 H c R 2 d )HfX 2 . The second catalyst compound includes at least one of the following general formulas:

    In both catalyst systems, the R groups can be independently selected from any number of substituents, including, for example, H, a hydrocarbyl group, a substituted hydrocarbyl group, or a heteroatom group, among others.

    PRODUCING POLYOLEFIN PRODUCTS
    10.
    发明公开
    PRODUCING POLYOLEFIN PRODUCTS 审中-公开
    生产聚烯烃产品

    公开(公告)号:EP3105259A2

    公开(公告)日:2016-12-21

    申请号:EP15705881.9

    申请日:2015-02-10

    Abstract: Polymers, and systems and methods for making and using the same are described herein. A polymer includes ethylene and at least one alpha olefin having from 4 to 20 carbon atoms. The polymer has a melt index ratio (MIR) greater than about 40. The polymer also has a value for Mw1/Mw2 of at least about 2.0, wherein Mw1/Mw2 is a ratio of a weight average molecular weight (Mw) for a first half of a temperature rising elution (TREF) curve from a cross-fractionation (CFC) analysis to an Mw for a second half of the TREF curve. The polymer also has a value for Tw1−Tw2 of less than about −15° C., wherein Tw1−Tw2 is a difference of a weight average elution temperature (Tw) for the first half of the TREF curve to a Tw for the second half of the TREF curve.

    Abstract translation: 催化剂体系及其制备和使用方法。 提供了一种使得催化剂组合物甲基化的方法,同时基本上正常化了异构体分布。 该方法包括将有机金属化合物在二甲氧基乙烷(DME)中浆化,并加入RMgBr在DME中的溶液,其中R是甲基或苄基,并且其中RMgBr相对于有机金属化合物大于约2.3当量。 在添加RMgBr之后,浆料混合至少约四小时。 烷基化的有机金属被分离出来,其中甲基化的物质具有介于约0.9和约1.2之间的内消旋/外消旋比。

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