发明授权
US08759243B2 Multi-component catalyst systems and polymerization processes for forming in-situ heterophasic copolymers and/or varying the xylene solubles content of polyolefins
有权
用于形成原位多相共聚物和/或改变二甲苯可溶物的多组分催化剂体系和聚合方法聚烯烃含量
- 专利标题: Multi-component catalyst systems and polymerization processes for forming in-situ heterophasic copolymers and/or varying the xylene solubles content of polyolefins
- 专利标题(中): 用于形成原位多相共聚物和/或改变二甲苯可溶物的多组分催化剂体系和聚合方法聚烯烃含量
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申请号: US13180672申请日: 2011-07-12
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公开(公告)号: US08759243B2公开(公告)日: 2014-06-24
- 发明人: Tim Coffy , Michel Daumerie , Kenneth Blackmon , William J. Gauthier , Jun Tian , Joseph L. Thorman
- 申请人: Tim Coffy , Michel Daumerie , Kenneth Blackmon , William J. Gauthier , Jun Tian , Joseph L. Thorman
- 申请人地址: US TX Houston
- 专利权人: Fina Technology, Inc.
- 当前专利权人: Fina Technology, Inc.
- 当前专利权人地址: US TX Houston
- 主分类号: C08F4/653
- IPC分类号: C08F4/653 ; C08F4/6592 ; C08F210/06
摘要:
Embodiments of the invention generally include multi-component catalyst systems, polymerization processes and heterophasic copolymers formed by the processes. The multi-component catalyst system generally includes a first catalyst component selected from Ziegler-Natta catalyst systems including a diether internal electron donor and a metallocene catalyst represented by the general formula XCpACpBMAn, wherein X is a structural bridge, CpA and CpB each denote a cyclopentadienyl group or derivatives thereof, each being the same or different and which may be either substituted or unsubstituted, M is a transition metal and A is an alkyl, hydrocarbyl or halogen group and n is an integer between 0 and 4. The multi-component catalyst system further includes a second catalyst component generally represented by the formula XCpACpBMAn, wherein X is a structural bridge, CpA and CpB each denote a cyclopentadienyl group or derivatives thereof, each being the same or different and which may be either substituted or unsubstituted, M is a transition metal and A is an alkyl, hydrocarbyl or halogen group and n is an integer between 0 and 4 and wherein the second catalyst component exhibits a higher ethylene response than the first catalyst component.
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