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    • 12. 发明授权
    • Process for the preparation of creep-resistant polypropylene block copolymers
    • 抗蠕变聚丙烯嵌段共聚物的制备方法
    • US06221974B1
    • 2001-04-24
    • US09171434
    • 1998-12-21
    • Mika HärkönenBo MalmAnders Nymark
    • Mika HärkönenBo MalmAnders Nymark
    • C08F29706
    • F16L9/133F16L57/02
    • The invention relates to a process for the preparation of a creep-resistant polypropylene by means of the following steps: (a) copolymerizing propylene and ethylene into a random copolymer at 40 to 110° C. using: a catalyst system of the above-mentioned type; a portion of ethylene or C4-C10-&agr;-olefin leading to 1.0 to 10.0% by weight of ethylene repeating units in said random copolymer; and no or a minimal amount of hydrogen leading to a MFR10 value of between 0.01 and 5.0 g/10 min for said random copolymer, if this step is performed first, or to a MFR2 value for said polypropylene of between 0.05 and 0.40 g/10 min, if this step is performed after step (b); the proportion of random copolymer of this step being from 20 to 80% by weight of said polypropylene, (b) polymerizing propylene at 40 to 110° C. using: a catalyst system of the above-mentioned type; no or a minimal portion of ethylene leading to 0.0 to 1.0% by weight of ethylene repeating units in the polymer resulting from this step; and an amount of hydrogen leading to a MFR2 value of between 30 and 300 g/10 min for said polymer, if this step is performed first, or to a MFR2 value for said polypropylene of between 0.05 and 0.40 g/10 min, if this step is performed after step (a); the proportion of polymer of this step being from 80 to 20% by weight of said polypropylene.
    • 本发明涉及一种通过以下步骤制备耐蠕变聚丙烯的方法:(a)在40-110℃下将丙烯和乙烯共聚到无规共聚物中,使用上述的催化剂体系 类型; 一部分乙烯或C4-C10-α-烯烃,导致所述无规共聚物中的乙烯重复单元的重量比为1.0-10.0% 并且对于所述无规共聚物,如果首先进行该步骤,或者对于所述聚丙烯的MFR 2值为0.05-0.40g / 10min,则没有或最小量的氢导致MFR10值在0.01-5.0g / 10min之间 min,如果在步骤(b)之后执行该步骤; 该步骤的无规共聚物的比例为所述聚丙烯的20至80重量%,(b)在40至110℃下聚合丙烯,使用上述类型的催化剂体系; 乙烯的无或最小部分导致由该步骤得到的聚合物中的乙烯重复单元为0.0-1.0重量% 如果该步骤首先进行,则导致所述聚合物的MFR 2值为30-300g / 10分钟的氢气量,或者对于所述聚丙烯的MFR 2值为0.05-0.40g / 10min,如果这样 在步骤(a)之后执行步骤; 该步骤的聚合物的比例为所述聚丙烯的80至20重量%。
    • 17. 发明授权
    • Propylene composition with high stiffness and impact strength
    • 丙烯组合物具有高刚度和冲击强度
    • US08759452B2
    • 2014-06-24
    • US13129511
    • 2010-02-04
    • Markus GahleitnerBo MalmKlaus BernreitnerJuliane Braun
    • Markus GahleitnerBo MalmKlaus BernreitnerJuliane Braun
    • C08J3/22C08F290/14C08L23/00C08F110/02
    • C08F10/00C08F10/06C08F110/06C08F4/6543C08F4/6492C08F4/651C08F210/16C08F2500/04C08F2500/19C08F2500/12C08F2500/11C08F2500/20C08F2500/24
    • The present invention is directed to a polypropylene composition comprising a propylene homo- or copolymer (A) with a polydispersity index (PI), determined according ISO 6721-1, of at least 5.8 Pa−1; and an inorganic filler (B) in an amount from 2.0 to 20 parts per weight based on 100 parts per weight of (A)+(B); The present invention is furthermore directed to a polypropylene composition comprising a propylene homo- or copolymer (A); and an inorganic filler (B); whereby the following relation is fulfilled (80F+1700)MPa≦T wherein F are the parts per weight of component (B) based on 100 parts per weight of the total amount of (A)+(B). T is the tensile modulus in MPa, determined according to ISO 527-2, of the polypropylene composition measured on a test specimen prepared by injection molding according to ISO 1873-2. The present invention is also directed to a process for the production of the polypropylene compositions according to the invention and to an article made of the polypropylene compositions according to the invention.The present invention is furthermore directed to the use of the polypropylene compositions according to the invention for the production of pipes, car components, appliance housings, transport containers.
    • 本发明涉及一种聚丙烯组合物,其包含根据ISO 6721-1测定的至少5.8Pa-1的具有多分散指数(PI)的丙烯均聚物或共聚物(A) 和每100重量份(A)+(B))为2.0〜20重量份的无机填料(B)。 本发明还涉及包含丙烯均聚物或共聚物(A)的聚丙烯组合物; 和无机填料(B); 由此满足以下关系(80F + 1700)MPa< NlE; T其中F是基于(A)+(B)的总量的每100重量份的组分(B)的重量份数。 T是根据ISO 527-2测定的根据ISO 1873-2通过注射成型制备的试样上测量的聚丙烯组合物的拉伸弹性模量(MPa)。 本发明还涉及一种生产根据本发明的聚丙烯组合物和由本发明的聚丙烯组合物制成的制品的方法。 本发明还涉及根据本发明的聚丙烯组合物用于生产管道,汽车部件,电器外壳,运输容器的用途。
    • 18. 发明授权
    • Pressureless polymer pipe, a compositon therefore, and a process for preparing it
    • 因此,无压聚合物管,组合物及其制备方法
    • US08563109B2
    • 2013-10-22
    • US11661574
    • 2005-08-30
    • Carl-Gustaf EkBo MalmOlli Tuominen
    • Carl-Gustaf EkBo MalmOlli Tuominen
    • B32B1/08C08L23/14C08L23/16C08L23/20
    • F16L9/147C08F210/06C08F210/16C08L23/12C08L23/14Y10T428/139C08F2/001C08L2666/06C08F2500/17C08F2500/12C08F2500/13
    • A pressureless polymer pipe, a composition therefore, and a process of preparing the composition are described. The pipe is characterized in that the polymer comprises a propylene polymer composition where the propylene base polymer is a heterophasic propylene copolymer having a matrix of a propylene homopolymer and a dispersed phase of an elastomeric copolymer of propylene and at least one olefin comonomer; has a comonomer content of 2-7% by weight, based on the weight of the heterophasic propylene copolymer; has a melt flow rate MFR (2/230), determined according to ISO 1133 C4, of 0.1-2.0 g/10 min; has a broad molecular weight distribution as defined by its rheology shear thinning index, SHI0/50, measured at 200° C. of 9-30; has a tensile modulus, determined according to ISO 527-2/1B at 1 mm/min and 23° C. of at least 1800 MPa; has an impact strength, determined according to ISO 179/1 eA of at least 6 kJ/m2 at 0° C. and at least 2 kJ/m2 at −20° C. The composition is a polymer composition as defined above. The process is characterized by polymerizing in the presence of a stereospecific Ziegler-Natta catalyst including an electron donor:(i) a propylene homopolymer matrix in at least one loop reactor at a temperature of at least 80° C. and a pressure of 4600-10000 kPa; and (ii) an elastomeric copolymer of propylene and at least one olefin comonomer in at least one gas-phase reactor at a lower temperature than in stage (i); to obtain a base polymer of heterophasic propylene copolymer as defined above.
    • 描述了无压聚合物管,组合物和制备该组合物的方法。 管的特征在于聚合物包括丙烯聚合物组合物,其中丙烯基聚合物是具有丙烯均聚物基质和丙烯与至少一种烯烃共聚单体的弹性体共聚物的分散相的多相丙烯共聚物; 基于多相丙烯共聚物的重量,共聚单体含量为2-7重量%; 具有根据ISO 1133 C4测定的熔体流动速率MFR(2/230)为0.1-2.0g / 10min; 具有由流变剪切稀化指数SHI0 / 50定义的宽分子量分布,其在200℃下测量为9-30; 具有根据ISO 527-2 / 1B在1mm / min和23℃下测定的至少1800MPa的拉伸模量; 具有根据ISO 179/1eA在0℃下测定为至少6kJ / m 2和-20℃下至少2kJ / m 2的冲击强度。组合物是如上所定义的聚合物组合物。 该方法的特征在于在包含电子给体的立体特异性齐格勒 - 纳塔催化剂存在下聚合:(i)至少一个环管反应器中的丙烯均聚物基质,温度至少为80℃,压力为4600- 10000 kPa; 和(ii)在低于阶段(i)的温度下,在至少一个气相反应器中的丙烯和至少一种烯烃共聚单体的弹性体共聚物; 以获得如上所定义的异相丙烯共聚物的基础聚合物。