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1. 发明申请

WO2009077031A1 REMOVING VOLATILE COMPOUNDS FROM POLYMER PELLETS 审中-公开
标题翻译：从聚合物颗粒中去除挥发性化合物
公开(公告)号：WO2009077031A1
公开(公告)日：2009-06-25
申请号：PCT/EP2008/009029
申请日：2008-10-24
申请人： BOREALIS TECHNOLOGY OY , KARBASI, Amir , KORHONEN, Esa , HIETANEN, Ensio , KNUDSEN, Karin, H. , HAGANE, Kai , BERGMANN, Fred , NYFORS, Klaus
发明人： KARBASI, Amir , KORHONEN, Esa , HIETANEN, Ensio , KNUDSEN, Karin, H. , HAGANE, Kai , BERGMANN, Fred , NYFORS, Klaus
IPC分类号： B29B9/16 , B29C71/00 , C08F6/00
CPC分类号： B29C71/0009 , B29B9/16 , B29C2071/0027 , B29C2071/0036 , B29K2023/12 , C08F6/005
摘要： The invention is directed to a process for the treatment of plastic material comprising a) providing a liquid; b) contacting the plastic material with the liquid; c) keeping the plastic material in the liquid at Tb-25°C to Tb of the liquid, wherein Tb is the boiling point of the liquid at the applied pressure; and d) removing the plastic material from the liquid. Furthermore, the invention is directed to the use of a liquid for the treatment of plastic material and to a plant for treating plastic material with a liquid.
摘要翻译：本发明涉及一种用于处理塑料材料的方法，包括：a）提供液体; b）将塑料材料与液体接触; c）将塑料材料保持在液体的Tb-25℃至Tb的液体中，其中Tb是施加压力下液体的沸点; 和d）从液体中去除塑料材料。此外，本发明涉及使用液体来处理塑料材料和用于用液体处理塑料材料的设备。

2. 发明申请

WO2011066892A1 PROCESS FOR PRODUCING POLYOLEFINS 审中-公开
标题翻译：生产聚烯烃的方法
公开(公告)号：WO2011066892A1
公开(公告)日：2011-06-09
申请号：PCT/EP2010/006703
申请日：2010-11-03
申请人： BOREALIS AG , KOKKO, Tapio , ELOVAINIO, Erno , KIVELÄ, Jouni , NYFORS, Klaus , HAGANE, Kai
发明人： KOKKO, Tapio , ELOVAINIO, Erno , KIVELÄ, Jouni , NYFORS, Klaus , HAGANE, Kai
IPC分类号： C08F6/00 , C08F10/00 , C08F2/34 , C08F2/00 , C08L23/00
CPC分类号： B01J8/1809 , B01J8/007 , B01J8/26 , B01J2208/00256 , B01J2208/00274 , B01J2208/0084 , B01J2219/0004 , C08F6/001 , C08F10/06 , C08F110/06 , C08F210/06 , C08L23/00 , C08F2/001 , C08F2/34 , C08F210/16
摘要： The present invention deals with a process of producing a polymer of at least one olefin in two consecutive reactors in gas phase in the presence of an olefin polymerisation catalyst where an olefin is polymerised in a first polymerization reactor in the presence of an olefin polymerisation catalyst and a first reaction gas mixture to form a fluidized bed comprising an olefin polymer and said first reaction gas mixture. The first reaction gas mixture together with the olefin polymer is continuously or intermittently withdrawn from the first polymerisation reactor and directed into a separation vessel so that a bed of polymer is formed in said separation vessel. A portion of said first reaction gas mixture is withdrawn from said separation vessel and returned into the first polymerization reactor to a point where the pressure is lower than in the separation vessel. The olefin polymer is withdrawn from said separation vessel to form a second product stream and the second product stream is directed into a second polymerization reactor. A second gas may be introduced into the bottom part of the separation vessel to avoid the carry-over of the reactants from the first polymerisation stage into the second polymerisation stage.
摘要翻译：本发明涉及一种在烯烃聚合催化剂存在下，在两相连续反应器中制备至少一种烯烃聚合物的方法，其中烯烃在烯烃聚合催化剂存在下在第一聚合反应器中聚合，第一反应气体混合物以形成包含烯烃聚合物和所述第一反应气体混合物的流化床。将第一反应气体混合物与烯烃聚合物一起连续地或间歇地从第一聚合反应器中取出并引导到分离容器中，使得在所述分离容器中形成聚合物床。将所述第一反应气体混合物的一部分从所述分离容器中取出并返回到第一聚合反应器中至压力低于分离容器的点。从所述分离容器中取出烯烃聚合物以形成第二产物流，将第二产物流引入第二聚合反应器。可以将第二气体引入分离容器的底部，以避免反应物从第一聚合阶段进入第二聚合阶段。

3. 发明申请

WO2007025640A1 PROCESS FOR POLYMERIZING OLEFINS IN THE PRESENCE OF AN OLEFIN POLYMERIZATION CATALYST 审中-公开
标题翻译：在烯烃聚合催化剂存在下聚合烯烃的方法
公开(公告)号：WO2007025640A1
公开(公告)日：2007-03-08
申请号：PCT/EP2006/007854
申请日：2006-08-08
申请人： BOREALIS TECHNOLOGY OY , ANDTSJÖ, Henrik , BERGSTRA, Michiel , KARLSSON, Ralf , NYFORS, Klaus , THORNGREN, Urban
发明人： ANDTSJÖ, Henrik , BERGSTRA, Michiel , KARLSSON, Ralf , NYFORS, Klaus , THORNGREN, Urban
IPC分类号： C08F10/00 , C08F2/34 , C08F2/14 , C08F2/00 , C08L23/00
CPC分类号： C08F210/16 , C08F2/34 , C08F2/001 , C08F2/14 , C08F210/08 , C08F2500/12 , C08F2500/03 , C08F2500/02 , C08F2500/01
摘要： The present invention relates to a process for the preparation of multimodal ethylene homo- or copolymers in at least two stages, the process comprising preparation of a first ethylene homo- or copolymer fraction in a loop reactor in slurry phase, preparation of a second ethylene homo- or copolymer fraction in a gas phase reactor, by using a catalyst not containing an inorganic oxide support, and operating the gas phase reactor in such conditions that at least part of the gas is recycled, and that at least a part of the recycled gas is condensed and the (partially) condensed gas is re-introduced into the gas phase reactor.
摘要翻译：本发明涉及在至少两个阶段制备多峰乙烯均聚物或共聚物的方法，该方法包括在淤浆相中的环管反应器中制备第一乙烯均聚物或共聚物部分，制备第二乙烯均聚物 - 或气相反应器中的共聚物部分，通过使用不含无机氧化物载体的催化剂，并在使至少部分气体再循环的条件下操作气相反应器，并且至少部分循环气体被冷凝，并将（部分）冷凝的气体重新引入气相反应器。

4. 发明申请

WO2012116845A1 FLEXIBLE REACTOR ASSEMBLY FOR POLYMERIZATION OF OLEFINS 审中-公开
标题翻译：柔性反应器组件用于烯烃的聚合
公开(公告)号：WO2012116845A1
公开(公告)日：2012-09-07
申请号：PCT/EP2012/000961
申请日：2012-03-02
申请人： BOREALIS AG , ERIKSSON, Erik , BERGSTRA, Michiel , NYFORS, Klaus , WEICKERT, Günter
发明人： ERIKSSON, Erik , BERGSTRA, Michiel , NYFORS, Klaus , WEICKERT, Günter
IPC分类号： B01J8/24 , B01J8/38 , B01J19/24 , B01J8/18
CPC分类号： B01J8/388 , B01J8/1827 , B01J8/1872 , B01J19/2465 , B01J2208/00274 , B01J2219/0004 , B01J2219/00254 , C08F10/00 , C08F110/06 , C08F2500/12 , C08F2/34 , C08F2/01
摘要： The invention relates to a reactor assembly for the production of polymers including a fluidized bed reactor (1) comprising a bottom zone (5), a middle zone (6) and an upper zone (7), an inlet (8) for the fluidization gas located in the bottom zone (5), an outlet (9) for the fluidization gas located in the upper zone (7); the outlet (9) for the fluidization gas being coupled with the fluidized bed reactor (1) via inlet (8); the equivalent cross-sectional diameter of the bottom zone (5) being monotonically increasing with respect to the flow direction of the fluidization gas through the fluidized bed reactor; the middle zone (6) having an essentially constant equivalent cross-sectional diameter with respect to the flow direction of the fluidization gas through the fluidized bed reactor; the equivalent cross-sectional diameter of the upper zone (7) being monotonically decreasing with respect to the flow direction of the fluidization gas through the fluidized bed reactor; wherein that the ratio of the height of the fluidized bed reactor to the equivalent cross- sectional diameter of the middle zone of the fluidized bed reactor is from 2 to 10; and wherein there is an unobstructed passageway in the direction of flow of the fluidization gas through the fluidized bed reactor from the bottom zone (5) to the upper zone (7).
摘要翻译：本发明涉及一种用于生产聚合物的反应器组件，包括流化床反应器（1），其包括底部区域（5），中间区域（6）和上部区域（7），用于流化的入口（8）位于底部区域（5）中的气体，位于上部区域（7）中的用于流化气体的出口（9）; 用于流化气体的出口（9）通过入口（8）与流化床反应器（1）联接; 底部区域（5）的等效横截面直径相对于通过流化床反应器的流化气体的流动方向单调增加; 所述中间区域（6）具有相对于通过所述流化床反应器的流化气体的流动方向具有基本恒定的等效横截面直径; 上部区域（7）的等效横截面直径相对于通过流化床反应器的流化气体的流动方向单调减小; 其中流化床反应器的高度与流化床反应器的中间区域的等效横截面直径之比为2至10; 并且其中在从底部区域（5）到上部区域（7）的流化床反应器的流化气体的流动方向上存在无障碍通道。

5. 发明申请

WO2012116844A1 HIGH THROUGHPUT REACTOR ASSEMBLY FOR POLYMERIZATION OF OLEFINS 审中-公开
标题翻译：用于烯烃聚合的高通量反应器组件
公开(公告)号：WO2012116844A1
公开(公告)日：2012-09-07
申请号：PCT/EP2012/000960
申请日：2012-03-02
申请人： BOREALIS AG , WEICKERT, Günter , ERIKSSON, Erik , BERGSTRA, Michiel , NYFORS, Klaus
发明人： WEICKERT, Günter , ERIKSSON, Erik , BERGSTRA, Michiel , NYFORS, Klaus
IPC分类号： B01J8/24 , B01J8/38 , B01J19/24 , B01J8/18
CPC分类号： B01J8/1872 , B01J8/1827 , B01J8/388 , B01J19/2465 , B01J2208/00274 , B01J2219/0004 , B01J2219/00254 , B01J2219/1947 , C08F110/06 , C08F210/16
摘要： Reactor assembly for the production of polymers including a fluidized bed reactor (1) comprising a bottom zone (5), a middle zone (6) and an upper zone (7), an inlet (8) for the fluidization gas located in the bottom zone (5), an outlet (9) for the fluidization gas located in the upper zone (7); the outlet (9) for the fluidization gas being coupled with the fluidized bed reactor (1) via inlet (8) via a gas circulation line; means for separation of solids from gas (2) being connected to said gas circulation line; the equivalent cross-sectional diameter of the upper zone (7) being monotonically decreasing with respect to the flow direction of the fluidization gas through the fluidized bed reactor; the middle zone (6) having an essentially constant equivalent cross-sectional diameter with respect to the flow direction of the fluidization gas through the fluidized bed reactor; the equivalent cross-sectional diameter of the bottom zone (5) being monotonically increasing with respect to the flow direction of the fluidization gas through the fluidized bed reactor; characterized in that the ratio of the height of the fluidized bed reactor to the equivalent cross-sectional diameter of the middle zone of the fluidized bed reactor is from 2 to 10; and whereby said upper zone (7) is directly connected to said middle zone (6).
摘要翻译：用于生产包括流化床反应器（1）的聚合物的反应器组件包括底部区域（5），中间区域（6）和上部区域（7），用于位于底部的流化气体的入口（8）区域（5），用于位于上部区域（7）中的流化气体的出口（9）; 用于流化气体的出口（9）通过气体循环管线通过入口（8）与流化床反应器（1）相连; 用于从与所述气体循环管线连接的气体（2）分离固体的装置; 上部区域（7）的等效横截面直径相对于通过流化床反应器的流化气体的流动方向单调减小; 所述中间区域（6）具有相对于通过所述流化床反应器的流化气体的流动方向具有基本恒定的等效横截面直径; 底部区域（5）的等效横截面直径相对于通过流化床反应器的流化气体的流动方向单调增加; 其特征在于，流化床反应器的高度与流化床反应器的中间区域的等效横截面直径之比为2至10; 并且由此所述上部区域（7）直接连接到所述中间区域（6）。

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