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    • 1. 发明公开
    • Process for polymerizing olefin polymers in the presence of a catalyst system and a method of controlling the process
    • PROCESS FOR IN聚合烯烃的存在是聚合物,用于控制程序催化剂和方法
    • EP2617741A1
    • 2013-07-24
    • EP12151536.5
    • 2012-01-18
    • Borealis AG
    • Tuominen, OlliEk, Carl-GustavAlastalo, KaunoLeskinen, PauliLylyharju, HarriEriksson, ErikEriksson, VirginieKokko, EsaBäckman, MatsJohansson, Solveig
    • C08F10/00C08F2/00
    • C08F10/00B01J8/001B01J8/1809B01J8/222B01J8/224B01J2219/00198B01J2219/00213B01J2219/00218B01J2219/00231C08F110/06C08F2400/02C08F2/00C08F110/02C08F2500/12
    • The present invention provides a method of controlling a continuous polymerization process where at least one olefin is polymerized in a polymerization reactor in the presence of a catalyst comprising a solid catalyst component further comprising a transition metal, and an activator, said method comprising the steps of:
      (i) providing a set point for the feed rate of said solid catalyst component into the polymerization reactor;
      (ii) providing a set point for a ratio of the activator feed rate to the solid catalyst component feed rate;
      (iii) controlling the feed rate of said solid catalyst component into the polymerization reactor to follow said set point for the feed rate of said solid catalyst component;
      (iv) calculating a set point for the feed rate of said activator from said set point for the feed rate of said solid catalyst component and said set point for the ratio of the activator feed rate to the solid catalyst component feed rate;
      (v) controlling the feed rate of said activator into the polymerization reactor to follow said set point for the feed rate of said activator.
      The present method results in a stable operation of the polymerization reactor and allows the production of polymers having consistent product properties.
    • 本发明提供一种控制连续聚合方法,其中至少一种烯烃进行聚合的聚合反应器中在一种催化剂,包含一种固体催化剂组分进一步包括一种过渡金属的存在的方法,以及在活化剂,所述方法包括如下步骤 (i)提供用于所述的固体催化剂组分加入到聚合反应器的进料速率的一组点; (ii)提供用于活化剂的进料速率加入到固体催化剂组分进料速率之比的设定点; (三)控制所述的固体催化剂组分的进料速率到聚合反应器跟随所述设定点为所述固体催化剂组分的进料速率; (iv)计算用于从设定点为所述固体催化剂成分的所述进料速率所述活化剂的进料速率为活化剂的进料速率加入到固体催化剂组分的进料速率的所述比率设定点和设定点; (V)控制所述活化剂的进料速度加入聚合反应器跟随所述设定点对于所述活化剂的进料速率。 本发明的方法产生稳定操作的聚合反应器中,并允许生产具有一致的产品性能的聚合物。
    • 3. 发明授权
    • PROCESS FOR THE PREPARATION OF FLOWABLE COMONOMER RICH POLYPROPYLENE
    • 共聚单体复方聚丙烯(Verfahrenfürfließfähiges)
    • EP2368921B1
    • 2014-11-26
    • EP10157879.7
    • 2010-03-26
    • Borealis AG
    • 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 ±-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 ±-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,所述组合物包含衍生自丙烯的单元和至少一种除了丙烯以外的至少一个C 2至C 20±α-烯烃,其量通过傅立叶变换红外光谱法测量至少为4.0重量%,并且给出 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 在第二反应器中在第一聚丙烯的存在下生产第二聚丙烯,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的单元和至少一种除丙烯之外的至少一个C2至C20-烯烃 至少9.0重量%的量将所述第一聚丙烯组合物转移到第三反应器中, - 在所述第三反应器中在所述第一聚丙烯组合物 第三聚丙烯,从而获得聚丙烯组合物,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,或所述第二聚丙烯的非晶部分(AM)的特性粘度(IV) 第三聚丙烯的二甲苯冷可溶(XCS)馏分为至少3dl / g。
    • 4. 发明公开
    • Process of flowable comonomer rich polypropylene
    • VERFAHREN ZUR HERSTELLUNG VONFLIEßFÄHIGEM,COMONOMERREICHEN POLYPROPYLEN
    • EP2368921A1
    • 2011-09-28
    • EP10157879.7
    • 2010-03-26
    • Borealis AG
    • 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 α-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 α-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,所述组合物包含衍生自丙烯的单元和至少一种除了丙烯以外的至少一个C 2至C 20±α-烯烃,其量通过傅立叶变换红外光谱法测量至少为4.0重量%,并且给出 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 在第二反应器中在第一聚丙烯的存在下生产第二聚丙烯,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的单元和至少一种除丙烯之外的至少一个C2至C20-烯烃 至少9.0重量%的量将所述第一聚丙烯组合物转移到第三反应器中, - 在所述第三反应器中在所述第一聚丙烯组合物 第三聚丙烯,从而获得聚丙烯组合物,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,或所述第二聚丙烯的非晶部分(AM)的特性粘度(IV) 第三聚丙烯的二甲苯冷可溶(XCS)馏分为至少3dl / g。
    • 7. 发明公开
    • A polyolefin preparation process with reduced tendency to reactor fouling
    • Verfahren zur Polyolefinherstellung mit reduzierter Tendenz zur Reaktorfaulung
    • EP2192133A1
    • 2010-06-02
    • EP08168572.9
    • 2008-11-07
    • Borealis AG
    • 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 polyolefin, 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,其包含(i)式(I)的过渡金属化合物€ƒ€ƒ€ƒ€ƒ€ƒ€ƒ€ƒ€ƒ€ƒ€ƒ€ƒ€ƒ(I) 其中M是元素周期表(IUPAC)中任何3至10族的过渡金属,每个X独立地是一价阴离子配体,每个L独立地是与过渡金属M相配的有机配体,R是 连接两个有机配体(L)的桥连基团,m为1,2或3,n为0,1或2,q为1,2或3,m + q等于过渡金属M的化合价, (ii)包含周期表第13族金属M'(IUPAC)的助催化剂,该固体催化剂组合物具有孔隙率 y根据ASTM 4641测量小于1.40ml / g,防污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。