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公开(公告)号:US08293857B2
公开(公告)日:2012-10-23
申请号:US12734585
申请日:2008-10-15
申请人: Alain Berardi , Andre Frederich , Dominique Jan , Jean-Jacques Kuhlburger , Anthony Sgard , Alain Van Daele
发明人: Alain Berardi , Andre Frederich , Dominique Jan , Jean-Jacques Kuhlburger , Anthony Sgard , Alain Van Daele
CPC分类号: C08F10/02 , C08F110/02 , C08F210/16 , C08F4/6492 , C08F4/6426 , C08F2500/12 , C08F210/14
摘要: Process for polymerization of ethylene using a catalyst system including (i) a solid catalyst of Ti, Mg and halogen, (ii) a first activator which is at least one trialkylaluminium compound of the formula AlR3, where each R is independently a C2 to C20 alkyl radical, and (iii) a second activator which is at least one alkylaluminium chloride of the formula AlR′2Cl, where each R′ is independently a C2 to C20 alkyl radical. The second activator is introduced directly into the polymerization reactor, without precontact with the solid catalyst, continuously or semi-continuously, and at a maximum rate of introduction at any time corresponding to less than 10 ppm by weight of chlorine relative to the rate of polyethylene production.
摘要翻译: 使用包括(i)Ti,Mg和卤素的固体催化剂的催化剂体系聚合乙烯的方法,(ii)第一活化剂,其为至少一种式AlR 3的三烷基铝化合物,其中每个R独立地为C 2至C 20 烷基,和(iii)第二活化剂,其为至少一种式AlR'2Cl的烷基氯化铝,其中每个R'独立地为C 2至C 20烷基。 将第二活化剂直接引入聚合反应器中,无需与固体催化剂预连接,连续或半连续,并且在任何相应于低于10ppm重量的氯的聚合物的最大引入速率相对于聚乙烯的速率 生产。
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公开(公告)号:US20100234543A1
公开(公告)日:2010-09-16
申请号:US12734585
申请日:2008-10-15
申请人: Alain Berardi , Andre Frederich , Jan Dominique , Jean-Jacques Kuhlburger , Anthony Sgard , Alain Van Daele
发明人: Alain Berardi , Andre Frederich , Jan Dominique , Jean-Jacques Kuhlburger , Anthony Sgard , Alain Van Daele
IPC分类号: C08F4/50
CPC分类号: C08F10/02 , C08F110/02 , C08F210/16 , C08F4/6492 , C08F4/6426 , C08F2500/12 , C08F210/14
摘要: The present invention relates to a process for polymerisation of ethylene, in particular a process which comprises using a catalyst system comprising comprising a catalyst system comprising: i) a solid catalyst comprising Ti, Mg and halogen, ii) a first activator which is at least one trialkylaluminium compound of the formula AIR3, where each R is independently a C2 to C20 alkyl radical, and iii) a second activator which is at least one alkylaluminium chloride of the formula AlR′2Cl, where each R′ is independently a C2 to C20 alkyl radical, characterised in that the second activator is introduced directly in the polymerisation reactor, without precontact with the solid catalyst, continuously or semi-continuously and at a maximum rate of introduction at any time corresponding to less than 10 ppm by weight of chlorine relative to the rate of polyethylene production.
摘要翻译: 本发明涉及一种聚合乙烯的方法,特别是包括使用包括催化剂体系的催化剂体系的方法,所述催化剂体系包含:i)包含Ti,Mg和卤素的固体催化剂,ii)至少第一活化剂 一种式为AIR3的三烷基铝化合物,其中每个R独立地为C 2至C 20烷基,和iii)第二活化剂,其为至少一种式AlR'2Cl的烷基氯化铝,其中每个R'独立地为C 2至C 20 烷基,其特征在于,第二活化剂直接在聚合反应器中引入,不与固体催化剂预接触,连续或半连续并且以最大引入速率在任何时间对应于小于10ppm重量的氯相对 达到聚乙烯生产率。
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