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1. 发明申请

WO2010037650A1 METHOD FOR CONTROLLING A PROCESS FOR POLYMERISATION OF AN OLEFIN 审中-公开
标题翻译：用于控制烯烃聚合方法的方法
公开(公告)号：WO2010037650A1
公开(公告)日：2010-04-08
申请号：PCT/EP2009/062180
申请日：2009-09-21
申请人： INEOS EUROPE LIMITED , CHAMAYOU, Jean-Louis , SERE PEYRIGAIN, Pierre
发明人： CHAMAYOU, Jean-Louis , SERE PEYRIGAIN, Pierre
IPC分类号： C08F2/00 , C08F2/34 , B01J8/18 , B01J8/24
CPC分类号： C08F210/16 , C08F2400/02 , C08F2/34 , C08F2/38 , C08F2/00 , C08F210/14 , C08F2500/12
摘要： The present invention relates to a method for controlling a process for polymerisation of an olefin, and in particular to a method for controlling a process for polymerising at least one olefin in a reaction zone, said process comprising in the reaction zone a reaction mixture and polymer particles, the reaction mixture comprising a principal olefin and at least one further reagent, and wherein the process is controlled using the ratio of at least one further reagent to principal olefin in the polymer particles in the reaction zone or in the amorphous phase of said polymer particles.
摘要翻译：本发明涉及一种用于控制烯烃聚合方法的方法，特别涉及用于控制在反应区中聚合至少一种烯烃的方法的方法，所述方法在反应区中包含反应混合物和聚合物颗粒，所述反应混合物包含主要烯烃和至少一种其它试剂，并且其中所述方法使用所述聚合物的反应区域或所述聚合物的非晶相中的聚合物颗粒中的至少一种其它试剂与主要烯烃的比率来控制粒子。

2. 发明申请

WO2005070976A1 POLYMERISATION PROCESS 审中-公开
标题翻译：聚合过程
公开(公告)号：WO2005070976A1
公开(公告)日：2005-08-04
申请号：PCT/GB2005/000157
申请日：2005-01-14
申请人： BP CHEMICALS LIMITED , JACOBSEN, Grant, Berent , LALANNE-MAGNE, Claudine, Viviane , SERE PEYRIGAIN, Pierre
发明人： JACOBSEN, Grant, Berent , LALANNE-MAGNE, Claudine, Viviane , SERE PEYRIGAIN, Pierre
IPC分类号： C08F210/16
CPC分类号： C08F210/16 , C08F10/00 , C08F2420/02 , C08F4/6592 , C08F210/14 , C08F2/34
摘要： A process for the copolymerisation of ethylene and an α-olefin having 7 to 10 carbon atoms in a fluidised bed gas phase reactor in the presence of a single site polymerisation catalyst comprises operating the process in condensed mode and wherein the amount of said α-olefin is maintained below that at which substantial condensation in the reactor occurs. The preferred α-olefin is 1-octene and the preferred single site polymerisation catalyst is a metallocene complex. By use of the process conditions of the present invention, higher α -olefins may be successfully employed in a gas phase process provided the amount of higher α -olefin comonomer is maintained below that at which substantial condensation occurs: Such operation is also dependent upon the operation temperature and the boiling point of the higher α-olefin and the process is particularly advantageous when performed in the presence of catalysts able to incorporate high levels of comonomers at low comonomer inventories.
摘要翻译：在单位聚合催化剂存在下，在流化床气相反应器中共聚乙烯和具有7至10个碳原子的α-烯烃的方法包括以缩合模式操作该方法，其中所述α-烯烃的量保持低于反应器发生大量冷凝的温度。优选的α-烯烃是1-辛烯，优选的单中心聚合催化剂是金属茂络合物。通过使用本发明的方法条件，如果高级α-烯烃共聚单体的量保持在低于发生实质性冷凝的量时，可以在气相方法中成功地使用较高级的α-烯烃：这种操作也取决于当在低共聚单体清单下能够并入高含量的共聚单体的催化剂存在下进行时，操作温度和较高级α-烯烃的沸点是特别有利的。

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