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    • 1. 发明申请
    • HETEROPHASIC PROPYLENE COPOLYMERS WITH IMPROVED STIFFNESS/IMPACT/FLOWABILITY BALANCE
    • 具有改善的强度/冲击/流动性平衡的异构丙烯共聚物
    • WO2012062734A1
    • 2012-05-18
    • PCT/EP2011/069611
    • 2011-11-08
    • BOREALIS AGLESKINEN, PauliDOSHEV, PetarKOCK, Cornelia
    • LESKINEN, PauliDOSHEV, PetarKOCK, Cornelia
    • C08L23/12C08F10/00C08F297/08
    • C08L23/14C08F110/06C08F210/06C08L23/12C08L2205/02C08L2205/025C08L2205/035C08L2207/02C08L2308/00C08L2314/02C08F10/06C08F2/001C08F2/14C08L23/16C08F4/6492C08F210/16C08F2500/12C08F2500/17C08F2500/04
    • Heterophasic propylene copolymer (HECO) comprising: (a) a polypropylene matrix comprising: (a 1 ) a first propylene homopolymer fraction (PPH1) with a melt flow rate MFR 2 (230°C) measured according to ISO 1133 in the range of > 200 to 500 g/10min, (a 2-1 ) a second propylene homopolymer fraction (PPH2) with a melt flow rate MFR 2 (230°C) measured according to ISO 1133 in the range of > 30 to ≤ 200 g/10min or, (a 2-2 ) a second propylene homopolymer fraction (PPH2) with a melt flow rate MFR 2 (230°C) measured according to ISO 1133 in the range of > 5 to ≤ 30 g/10min and, (a 3-1 ) a third propylene homopolymer fraction (PPH3) with a melt flow rate MFR 2 (230°C) measured according to ISO 1133 in the range of 0.03 to ≤ 5 g/10min, if the second propylene homopolymer fraction is fraction (a 2-1 ) or, (a 3-2 ) a third propylene homopolymer fraction (PPH3) with a melt flow rate MFR 2 (230°C) measured according to ISO 1133 in the range of > 30 to ≤ 200 g/10min, if the second propylene homopolymer fraction is fraction (a 2-2 ), wherein the polypropylene matrix has a melt flow rate MFR 2 (230°C) measured according to ISO 1133 in the range of 30 to 500 g/10min and a xylene cold soluble fraction determined at 23°C according to ISO 6427 in the range of 0.5 to 2 (230°C) measured according to ISO 1133 in the range of 25 to 200 g/10min and, (ii) the amorphous phase (AM) of the cold soluble fraction (XCS) of the heterophasic propylene copolymer has an intrinsic viscosity measured according to ISO 1628-1 (at 135°C in tetraline) of ≥ 2.0 dl/g, and a process for its preparation.
    • 异相丙烯共聚物(HECO),其包含:(a)聚丙烯基质,其包含:(a1)根据ISO 1133测量的熔体流动速率MFR 2(230℃)的第一丙烯均聚物部分(PPH1)的范围> 200至 500g / 10min,(a2-1)根据ISO 1133测量的熔体流动速率MFR 2(230℃)在> 30至= 200g / 10min范围内的第二丙烯均聚物部分(PPH2),或(a2 -2)根据ISO 1133在> 5至= 30g / 10min范围内测量的熔体流动速率MFR 2(230℃)的第二丙烯均聚物部分(PPH2),和(a3-1)第三丙烯均聚物 如果第二丙烯均聚物馏分为馏分(a2-1)或(a3-),则根据ISO 1133测量的馏分(PPH 3)的熔体流动速率MFR 2(230℃)为0.03至= 5g / 2)如果第二丙烯均聚物部分(如果第二丙烯均聚物部分)具有根据ISO 1133测量的熔体流动速率MFR 2(230℃)的范围> 30至= 200g / 10min的第三丙烯均聚物部分(PPH 3) 是分数(a2-2),其中聚丙烯基质的熔体流动速率MFR 2(230℃)根据ISO 1133测量的范围为30至500g / 10min,二甲苯冷可溶物级分在23℃下测定,根据 到ISO 6427,范围为0.5至<2.0wt%,(b)分散在所述基质中的弹性体丙烯共聚物,其中(i)所述多相丙烯共聚物具有根据ISO 1133测量的熔体流动速率MFR 2(230℃) 在25至200g / 10min的范围内,和(ii)多相丙烯共聚物的冷可溶级分(XCS)的无定形相(AM)具有根据ISO 1628-1测量的特性粘度(在135℃ 在四环素中)= 2.0dl / g,及其制备方法。
    • 7. 发明申请
    • RANDOM PROPYLENE COPOLYMERS FOR PIPES
    • 用于管道的随机丙烯共聚物
    • WO2011104100A1
    • 2011-09-01
    • PCT/EP2011/051611
    • 2011-02-03
    • Borealis AGBERGSTRA, MichielMALM, BoLESKINEN, PauliKOCK, CorneliaSUNDHOLM, Tua
    • BERGSTRA, MichielMALM, BoLESKINEN, PauliKOCK, CorneliaSUNDHOLM, Tua
    • C08L23/10
    • C08L23/10C08L2205/02C08L2666/06
    • Random propylene copolymer comprising (a) a first polypropylene being a first random propylene copolymer, said first random propylene copolymer has a melt flow rate MFR 10 (230 C) of not more than 1.5 g/10min, (b) a second polypropylene being a first propylene homopolymer or a second random propylene copolymer, (c) a third polypropylene being a second propylene homopolymer or a third random propylene copolymer, said third random propylene copolymer has a comonomer content of 0.5 to 3.5 wt. -%, wherein further (i) the first polypropylene differ from the second polypropylene and the third polypropylene by the melt flow rate MFR 2 (230 C) and/or by the comonomer content, (ii) the second polypropylene differ from the third polypropylene by the melt flow rate MFR 2 (230 C) and/or by the comonomer content [wt.-%], and (iii) the random propylene copolymer (R-PP) has a melt flow rate MFR 2 (230 C) of 0.05 to 10.00 g/10min.
    • 无规丙烯共聚物,其包含(a)第一无规丙烯共聚物的第一聚丙烯,所述第一无规丙烯共聚物的熔体流动速率MFR 10(230℃)不超过1.5g / 10min,(b)第二聚丙烯为第一 丙烯均聚物或第二无规丙烯共聚物,(c)第三聚丙烯是第二丙烯均聚物或第三无规丙烯共聚物,所述第三无规丙烯共聚物的共聚单体含量为0.5-3.5重量%。 - %,其中进一步(i)第一聚丙烯与第二聚丙烯和第三聚丙烯的熔体流动速率MFR 2(230℃)和/或共聚单体含量不同,(ii)第二聚丙烯与第三聚丙烯不同,第三聚丙烯通过 熔体流动速率MFR 2(230℃)和/或共聚单体含量[wt。-%],和(iii)无规丙烯共聚物(R-PP)的熔体流动速率MFR 2(230℃)为0.05-10.00 克/ 10分钟。
    • 8. 发明申请
    • PROCESS FOR PREPARING PROPYLENE POLYMERS WITH AN ULTRA HIGH MELT FLOW RATE
    • 制备具有超高熔体流动速率的丙烯聚合物的方法
    • WO2012062737A1
    • 2012-05-18
    • PCT/EP2011/069616
    • 2011-11-08
    • BOREALIS AGPAAVILAINEN, JuhaLESKINEN, Pauli
    • PAAVILAINEN, JuhaLESKINEN, Pauli
    • C08F210/06C08F4/646C08L23/10C08F4/649
    • C08F210/06C08L23/12C08F4/6492C08F2/001C08F4/6465C08L23/142
    • Process for the production of propylene homo- or copolymers with an MFR2 (230°C, 2.16kg, ISO 1133) in the range of 800 to 3000 g/1Omin, said process comprises the steps of a) polymerising propylene and optionally an ethylene and/or C 4 -C 12 alpha-olefin comonomer in a slurry reactor in the presence of a polymerisation catalyst system, obtaining as slurry reactor product a first propylene homo- or copolymer component with an MFR2 (230°C, 2.16kg, ISO 1133) in the range of 1000 to 4000 g/1Omin, b) transferring the slurry reactor product into a gas phase reactor c) further polymerising propylene and optionally an ethylene and/or C4-Ci2 alpha-olefin comonomer in the presence of said slurry reactor product and the polymerisation catalyst system d) optionally recovering the so produced propylene homo- or copolymer for further processing, said polymerisation catalyst system comprises (i) a Ziegler-Natta procatalyst (ii) an organometallic cocatalyst and (iii) an external donor represented by formula (I) Si(OCH 2 CH 3 ) 3 (NR 1 R 2 ) (I) wherein R1 and R2 can be the same or different and represent a hydrocarbon group having 1 to 12 carbon atoms; and the use of such prepared polymers for blow moulding applications.
    • 用于生产具有在800至3000g / 10min范围内的MFR 2(230℃,2.16kg,ISO 1133)的丙烯均聚物或共聚物的方法,所述方法包括以下步骤:a)将丙烯和任选的乙烯和 /或C 4 -C 12α-烯烃共聚单体在淤浆反应器中在聚合催化剂体系的存在下,获得作为浆料反应器产物的MFR 2(230℃,2.16kg,ISO 1133)的第一丙烯均聚物或共聚物组分 范围为1000至4000g / 10min,b)将淤浆反应器产物转移到气相反应器中c)在所述淤浆反应器产物存在下进一步聚合丙烯和任选的乙烯和/或C 4 -C 12α-烯烃共聚单体,和 聚合催化剂体系d)任选地回收如此生产的丙烯均聚物或共聚物进行进一步处理,所述聚合催化剂体系包括(i)齐格勒 - 纳塔前催化剂(ii)有机金属助催化剂和(iii)由fo表示的外部供体 (I)Si(OCH 2 CH 3)3(NR 1 R 2)(I)其中R 1和R 2可以相同或不同,表示具有1至12个碳原子的烃基; 以及使用这种制备的聚合物进行吹塑应用。