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    • 5. 发明申请
    • POLYMER COMPOSITION AND A PROCESS FOR PRODUCTION OF THE POLYMER COMPOSITION
    • 聚合物组合物和生产聚合物组合物的方法
    • WO2017207493A1
    • 2017-12-07
    • PCT/EP2017/062902
    • 2017-05-29
    • BOREALIS AG
    • LIU, YiSUMERIN, VictorTUPE, Ravindra
    • C08L23/08
    • A polyethylene composition comprising a base resin is disclosed herein. The base resin includes an ethylene homo- or copolymer fraction (A1), and an ethylene homo- or copolymer fraction (A2). Fraction (A1) has a lower weight average molecular weight than fraction (A2). The base resin has a melt flow rate MFR 21 of equal to or less than 8.0 g/10 min and a density of 930 to 950 kg/m3. The polyethylene composition has a melt flow rate MFR 5 of 0.01 to 0.3 g/10 min, a flow rate ratio FRR 21/5 of equal to or more than 20 and a ratio of the weight average molecular weight and the number average molecular weight (M w /M n ) of equal to or less than 30. Also the polyethylene composition has a tensile modulus of less than 1000 MPa. Also a process for the production of a polyethylene composition comprising polyethylene base resin is disclosed herein.
    • 本文公开了包含基础树脂的聚乙烯组合物。 基础树脂包括乙烯均聚物或共聚物部分(A1)和乙烯均聚物或共聚物部分(A2)。 级分(A1)具有比级分(A2)更低的重均分子量。 基础树脂具有等于或小于8.0g / 10min的熔体流动速率MFR 21和930至950kg / m 3的密度。 所述聚乙烯组合物具有0.01至0.3g / 10min的熔体流动速率MFR 5 5,等于或大于20的流率比FRR 21/5和 重均分子量与数均分子量(M w / M n)之比等于或小于30.此外,聚乙烯组合物的拉伸模量 小于1000MPa。 本文还公开了生产包含聚乙烯基础树脂的聚乙烯组合物的方法。
    • 6. 发明申请
    • PROCESS FOR PRODUCING POLYETHYLENE
    • 生产聚乙烯的方法
    • WO2016124676A1
    • 2016-08-11
    • PCT/EP2016/052354
    • 2016-02-04
    • BOREALIS AG
    • SUMERIN, VictorTHORMAN, JosephAHO, JaniVAHTERI, MarkkuTUPE, RavindraKELA, Jarmo
    • C08F210/16C08F4/646C08F2/34C08L23/08
    • C08F210/16C08L23/16C08F4/6465C08F2/001C08F210/14C08F2500/04C08F2500/12C08F2500/07C08F4/6492C08F4/6555
    • The present invention relates to a process for producing ethylene copolymers in a multistage process comprising at least one slurry phase polymerization stage and at least one gas phase polymerization stage in the presence of Ziegler Natta catalyst comprising a solid catalyst component, a cocatalyst of a compound of group 13 metal and an external additive selected from alkoxysilanes of formula (I) R 1 n Si(OR 2 ) 4-n , (I) where n is an integer 0 to 3, each R 1 are equal or different and are selected among H, halogen,alkyl groups of 1 to 6 10 carbon atoms optionally substituted with one or more halogen atoms,alkenyl groups of 2 to 6 carbon atoms optionally substituted with one or more halogen atoms, and aryl groups of 6 to 12 carbon atoms optionally substituted with one or more halogen atoms, or the R 1 groups can form with the Si atom they are linked to a ring of 3 to 8 ring atoms, provided that all R 1 are not hydrogen, R 2 are equal or different and are selected among alkyl groups of 1 to 6 carbon atoms optionally substituted with one or more halogen atoms, alkenyl groups of 2 to 6 carbon atoms optionally substituted with one or more halogen atoms, and aryl groups of 6 to 12 carbon atoms optionally substituted with one or more halogen atoms, or the OR 2 groups can form with the Si atom they are linked to a ring of 3 to 8 ring atoms, halogen is Br, Cl or F. The invention further relates to the catalysts and use thereof in said multistage process r for producing ethylene copolymers having melt flow rate ratio FRR 21/5 at least 40 and/or polydispersity index PDI of at least 27.
    • 本发明涉及在多级方法中生产乙烯共聚物的方法,该方法包括在齐格勒纳塔催化剂存在下的至少一个淤浆相聚合阶段和至少一个气相聚合阶段,该催化剂包含固体催化剂组分,化合物的助催化剂 第13族金属和选自式(I)的烷氧基​​硅烷的外加剂R 1 n Si(OR 2)4-n,(I)其中n为0至3的整数,每个R 1相同或不同,选自H,卤素, 任选被一个或多个卤素原子取代的1至6个10个碳原子的烷基,任选被一个或多个卤素原子取代的2至6个碳原子的烯基,以及6至12个碳原子的芳基,任选被一个或多个 卤素原子,或者R1基团可以与它们连接到3至8个环原子的环上的Si原子一起形成,条件是所有R 1不是氢,R 2相同或不同,并且选自1至6个碳原子的烷基 任选被一个或多个卤素原子取代的碳原子,任选被一个或多个卤素原子取代的2至6个碳原子的烯基和任选被一个或多个卤素原子取代的6至12个碳原子的芳基或OR 2基团 可以与它们连接到3至8个环原子的环上的Si原子形成,卤素是Br,Cl或F.本发明进一步涉及催化剂及其用于生产具有熔体流动速率的乙烯共聚物的多级方法 比FRR21 / 5至少40和/或多分散指数PDI至少27。
    • 9. 发明申请
    • GAS PHASE POLYMERIZATION PROCESS
    • 气相聚合方法
    • WO2015128469A1
    • 2015-09-03
    • PCT/EP2015/054149
    • 2015-02-27
    • BOREALIS AG
    • KANELLOPOULOS, VasileiosKRALLIS, ApostolosAL-HAJ ALI, MohammadTUPE, Ravindra
    • C08F2/01C08F2/34
    • C08F2/34C08F2/01C08F110/02
    • An olefin polymerization process comprising polymerizing olefins in gas phase in a fluidized bed in the presence of an olefin polymerization catalyst in a polymerization reactor having a vertical body; a generally conical downwards tapering bottom zone; a generally cylindrical middle zone having a height to diameter ratio L/D of at least 4, above and connected to said bottom zone; and a generally conical upwards tapering top zone above and connected to said middle zone wherein (i) fluidization gas is introduced to the bottom zone of the reactor from where it passes upwards through the reactor; (ii) the fluidization gas is withdrawn from the top zone of the reactor, filtered, compressed, cooled and returned into the bottom zone of the reactor; (iii) a fluidized bed is formed within the reactor where the growing polymer particles are suspended in the upwards rising gas stream; and (iv) there is no fluidization grid in the reactor; characterized in that the gas velocity is maintained in the reactor such that N Br is within the range of from 2.5 to 7.
    • 一种烯烃聚合方法,包括在具有垂直体的聚合反应器中,在烯烃聚合催化剂存在下,在流化床中气相聚合烯烃; 大致圆锥形的向下锥形底部区域; 大致圆柱形的中间区域,其高度与直径之比L / D至少为4,高于并连接到所述底部区域; 以及在所述中间区域上方并连接到所述中间区域的大致锥形的向上锥形顶部区域,其中(i)流化气体被引导到反应器的底部区域,从该区域向上通过反应器; (ii)流化气体从反应器的顶部区域排出,过滤,压缩,冷却并返回到反应器的底部区域; (iii)在反应器内形成流化床,其中生长的聚合物颗粒悬浮在向上升的气流中; 和(iv)反应器中不存在流化栅; 其特征在于,气体速度保持在反应器中,使得NBr在2.5至7的范围内。