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    • 22. 发明申请
    • METHOD FOR THE DOSAGE OF A FLUIDIZED POLYMERIZATION CATALYST INTO A POLYMERIZATION REACTOR
    • 将聚合催化剂流化成聚合反应器的方法
    • WO1992016747A1
    • 1992-10-01
    • PCT/FI1992000080
    • 1992-03-20
    • NESTE OYKOSKINEN, JukkaNYFORS, KlausLESKINEN, Pauli
    • NESTE OY
    • F04B07/06
    • B01J8/003B01J8/002B01J8/0035F04B7/06
    • The dosage pump according to the invention comprises a cylinder (2), a piston (4) moving back and forth in it and openable and closable inlet (5) and outlet (6) opening in the piston-swept space (3). The opening and closing of the openings mentioned are carried out by an intermediate pipe (7) arranged movably, and with respect thereto tightly, between the cylinder (2) and the mantles of the piston (4). The transmission opening (8) of the intermediate pipe (7) is transferred by moving the intermediate pipe (7) upon the inlet (5) and the outlet (6) opening, the whole surface of the intermediate pipe always covering one of the inlet (5) and outlet (6) openings mentioned. The dosage pump mentioned can preferably be applied for the dosage of hard-flowing substances, e.g. for feeding solid catalyst or wax into olefin polymerization reactor.
    • 根据本发明的剂量泵包括气缸(2),在其中前后移动的活塞(4)和在活塞扫掠空间(3)中开口的可开启和关闭的入口(5)和出口(6)。 所述开口的打开和关闭由中间管道(7)进行,所述中间管道(7)在所述气缸(2)和所述活塞(4)的外壳之间可移动地并相对于其紧密配置。 通过在入口(5)和出口(6)开口处移动中间管(7)来转移中间管(7)的传动开口(8),中间管的整个表面总是覆盖入口 (5)和出口(6)开口。 所提及的剂量泵可以优选用于硬流动物质的剂量,例如 用于将固体催化剂或蜡进料到烯烃聚合反应器中。
    • 23. 发明申请
    • RANDOM PROPYLENE COPOLYMER WITH HIGH STIFFNESS AND LOW HAZE
    • 随机丙烯共聚物,具有高刚度和低湿度
    • WO2012159927A1
    • 2012-11-29
    • PCT/EP2012/058985
    • 2012-05-15
    • BOREALIS AGPOTTER, ElisabethDOSHEW, PetarKHEIRANDISH, SaeidLESKINEN, PauliGAHLEITNER, Markus
    • POTTER, ElisabethDOSHEW, PetarKHEIRANDISH, SaeidLESKINEN, PauliGAHLEITNER, Markus
    • F01D5/02F01D5/34C08L23/14
    • C08L23/142C08F210/06C08F210/16C08F2500/12C08F2/34C08F2/14C08F2/001
    • Process for the preparation of a propylene copolymer, said process is a sequential polymerization process comprising at least two reactors connected in series, wherein said process comprises the steps of (A) polymerizing in a first reactor propylene and optionally ethylene and /or a C 4 to C 12 a-olefin, obtaining a polypropylene fraction (A), (B) transferring said polypropylene fraction (A) and unreacted comonomers from the first reactor into a second reactor, (C) feeding to said second reactor propylene and ethylene and /or a C4 to C12 a-olefin, (D) polymerizing in said second reactor and in the presence of said polypropylene fraction (A) propylene and ethylene and /or a C 4 to C 12 a-olefin, obtaining a propylene copolymer fraction (B), said polypropylene fraction (A) and said propylene copolymer fraction (B) form the propylene copolymer, wherein further the temperature in the first reactor (R-1) is of more than 70 °C to equal or below 90 °C, the temperature in the second reactor (R-2) is of equal or more than 80 °C to equal or below 95 °C, in the first reactor (R-1) and second reactor (R-2) the polymerization takes place in the presence of a solid catalyst system (SCS) having a surface area measured according to ASTM D 3662 of less than 30 m 2 /g and/or a pore volume measured according to ASTM 4641 of less than 1.0 ml/g, wherein further said solid catalyst system comprises a transition metal selected from one of the groups 4 to 6 of the periodic table (IUPAC), a metal which is selected from one of the groups 1 to 3 of the periodic table (IUPAC), and an internal electron donor (ID), and said propylene copolymer has a melt flow rate MFR 2 (230 °C) of equal or more than 65 to equal or below 200 g/lOmin, and a comonomer content in the range of equal or more than 1.5 to equal or below 8.0 wt.-%.
    • 制备丙烯共聚物的方法,所述方法是包含至少两个串联连接的反应器的顺序聚合方法,其中所述方法包括以下步骤:(A)在第一反应器中聚合丙烯和任选的乙烯和/或C 4至 得到聚丙烯馏分(A),(B)将所述聚丙烯馏分(A)和未反应的共聚单体从第一反应器转移到第二反应器中,(C)向第二反应器进料丙烯和乙烯和/或 (D)在所述第二反应器中和在所述聚丙烯级分(A)丙烯和乙烯和/或C 4至C 12α-烯烃存在下聚合,得到丙烯共聚物部分(B),所述 聚丙烯馏分(A)和所述丙烯共聚物部分(B)形成丙烯共聚物,其中第一反应器(R-1)中的温度进一步高于70℃至等于或低于90℃, 第二反应器(R-2 )等于或大于80℃至等于或低于95℃,在第一反应器(R-1)和第二反应器(R-2)中,聚合在固体催化剂体系(SCS)存在下进行, 具有根据ASTM D 3662测量的表面积小于30m 2 / g和/或根据ASTM 4641测量的孔体积小于1.0ml / g,其中所述固体催化剂体系还包含选自以下之一的过渡金属: 元素周期表(IUPAC)的第4至6族,选自元素周期表(IUPAC)中的1至3族之一的金属和内部电子给体(ID),所述丙烯共聚物具有熔体 等于或大于65的流量MFR 2(230℃)等于或低于200g / 10min,共聚单体含量在等于或大于1.5至等于或低于8.0重量%的范围内。
    • 25. 发明申请
    • PROCESS FOR THE PREPARATION OF FLOWABLE COMONOMER RICH POLYPROPYLENE
    • 制备流动性丰富的聚丙烯的方法
    • WO2011117224A1
    • 2011-09-29
    • PCT/EP2011/054312
    • 2011-03-22
    • BOREALIS AGTUOMINEN, OlliMALM, BoLESKINEN, Pauli
    • TUOMINEN, OlliMALM, BoLESKINEN, Pauli
    • C08F10/06C08F2/00C08F297/08C08L23/14C08F210/06
    • C08F210/06C08F110/06C08L23/14C08L23/16C08L2205/025C08L2205/03C08L2308/00C08F2/001C08F210/16C08F2500/12C08F2500/17
    • Process for producing a polypropylene composition, said composition comprises units derived from propylene and at least one C2 to C20 a -olefin other than propylene in an amount of at least 4.0 wt- % measured by Fourier transform infrared spectroscopy and given in wt.-%, and said process comprises the steps of producing in at least one first reactor a first polypropylene having a xylene cold soluble (XCS) content not exceeding 4.0 wt.-%, transferring said first polypropylene in a second reactor, producing in the second reactor in the presence of the first polypropylene a second polypropylene thereby obtaining a first polypropylene composition, said second polypropylene comprises units derived from propylene and at least one C2 to C20 a -olefin other than propylene in an amount of at least 9.0 wt-%, transferring said first polypropylene composition to a third reactor, producing in the third reactor in the presence of the first polypropylene composition a third polypropylene thereby obtaining the polypropylene composition, wherein said third polypropylene has a xylene cold soluble (XCS) content of below 9.0 wt- %, or • the intrinsic viscosity (IV) of the amorphous part (AM) of the xylene cold soluble (XCS) fraction of the third polypropylene is at least 3 dl/g.
    • 用于生产聚丙烯组合物的方法,所述组合物包含通过傅里叶变换红外光谱测量并且以重量%计的衍生自丙烯和至少一种丙烯以外的至少4.0重量%的至少4.0重量%的C 2 -C 20α-烯烃的单元, ,并且所述方法包括以下步骤:在至少一个第一反应器中生产具有不超过4.0重量%的二甲苯冷可溶物(XCS)含量的第一聚丙烯,在第二反应器中转移所述第一聚丙烯,在第二反应器中生产 第一聚丙烯存在第二聚丙烯,从而获得第一聚丙烯组合物,所述第二聚丙烯包含衍生自丙烯和至少一种量至少为9.0重量%的丙烯以外的至少一种C 2至C 20α-烯烃的单元,将所述 将第一聚丙烯组合物加入到第三反应器中,在第三聚丙烯组合物存在下在第三反应器中制备第三聚丙烯,由此得到 其中所述第三聚丙烯具有低于9.0重量%的二甲苯冷可溶物(XCS)含量,或者二甲苯冷可溶(XCS)部分的无定形部分(AM)的特性粘度(IV) 第三聚丙烯为至少3dl / g。
    • 27. 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。
    • 29. 发明申请
    • A POLYOLEFIN PREPARATION PROCESS WITH REDUCED TENDENCY TO REACTOR FOULING
    • 具有降低反应物浓度的聚烯烃制备方法
    • WO2010052267A1
    • 2010-05-14
    • PCT/EP2009/064674
    • 2009-11-05
    • BOREALIS AGHAKALA, KimmoNOOPILA, TuomasTUOMINEN, OlliLESKINEN, Pauli
    • HAKALA, KimmoNOOPILA, TuomasTUOMINEN, OlliLESKINEN, Pauli
    • C08F10/00C08F2/00C08F2/06C08F2/14
    • C08F10/00C08F110/06Y02P20/544C08F2/22C08F2/005C08F2/14C08F2500/18C08F2500/12
    • The present invention relates to a process for the preparation of a polyolefϊn, wherein ethylene and/or propylene are polymerised in a liquid or supercritical hydrocarbon reaction medium of a polymerisation reactor R1 in the presence of a solid catalyst composition and an antifouling composition, the solid catalyst composition comprising (i) a transition metal compound of formula (I) L m R n MX q (I) wherein M is a transition metal of anyone of the groups 3 to 10 of the periodic table (IUPAC), each X is independently a monovalent anionic σ-ligand, each L is independently an organic ligand which coordinates to the transition metal M, R is a bridging group linking two organic ligands (L), m is 1, 2 or 3, n is 0, 1 or 2, q is 1, 2 or 3, m+q is equal to the valency of the transition metal M, and (ii) a cocatalyst comprising a metal M' of Group 13 of the periodic table (IUPAC), the solid catalyst composition having a porosity measured according to ASTM 4641 of less than 1.40 ml/g, and the antifouling composition comprising an organic compound which has at least 14 carbon atoms and comprises at least one polar functional group.
    • 本发明涉及一种制备聚烯烃的方法,其中乙烯和/或丙烯在聚合反应器R1的液体或超临界烃反应介质中在固体催化剂组合物和防污组合物的存在下聚合, 固体催化剂组合物包含(i)式(I)的过渡金属化合物LmRnMXq(I)其中M是周期表(IUPAC)中第3至10族中任何一种的过渡金属,各X独立地是一价阴离子 每个L独立地是与过渡金属M配位的有机配体,R是连接两个有机配体(L)的桥连基团,m是1,2或3,n是0,1或2,q是 1,2或3,m + q等于过渡金属M的化合价,和(ii)包含周期表第13族金属M'的助催化剂(IUPAC),固体催化剂组合物具有测量的孔隙率 根据ASTM 4641小于1.40毫升/克,和防伪 该组合物包含具有至少14个碳原子并且包含至少一个极性官能团的有机化合物。