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    • 2. 发明授权
    • Highly flowable propylene block copolymers
    • 高流动性丙烯嵌段共聚物
    • US07196140B2
    • 2007-03-27
    • US10296256
    • 2001-05-23
    • Ulrich DahnWolfgang BidellHans-Jürgen ZimmermannRoland HingmannJoachim RöschGünther SchweierJürgen Oelze
    • Ulrich DahnWolfgang BidellHans-Jürgen ZimmermannRoland HingmannJoachim RöschGünther SchweierJürgen Oelze
    • C08F297/08C08F297/00C08F4/64C08F4/642
    • C08F297/08C08F10/06C08F110/06C08F210/06C08L53/00C08F2/001C08F2/34C08L2666/02C08F2500/12C08F2500/17C08F210/16
    • The invention relates to highly flowable propylene block copolymers that comprise 50 to 80 wt.-% of a propylene homopolymer and 10 to 70 wt.-% of a propylene copolymer having 5 to 50 wt.-% of a C2–C8 alk-1-ene polymerized into it that is different from propylene, and that are obtainable from the gaseous phase by a two-step polymerization by means of a Ziegler-Natta catalyst system. In a first polymerization step, the propylene is polymerized at a pressure of 10 to 50 bar, a temperature of 50 to 100° C. and an average dwelling time of the reaction mixture of 0.3 to 5 hours in the presence of at least 2.0% by volume, based on the total volume, of hydrogen. The propylene homopolymer obtained in said first polymerization step is transferred together with the Ziegler-Natta catalyst system into an intermediate container, expanded for 0.01 to 5 minutes to less than 5 bar and maintained at a temperature of 10 to 80° C. The pressure in the intermediate container is then increased by 5 to 60 bar by introducing under pressure a gaseous mixture, and the propylene homopolymer is then transferred to a second polymerization step together with the Ziegler-Natta catalyst system. In said second polymerization step, a mixture from propylene and a C2–C8 alk-1-ene is polymerized into the propylene homopolymer at a pressure of 10 to 50 bar, a temperature of 50 to 100° C. and an average dwelling time of 0.5 to 5 hours. The weight ratio between the monomers reacted in the first and those reacted in the second polymerization step are adjusted to be in the range of from 4:1 to 1:1.
    • 本发明涉及高流动性丙烯嵌段共聚物,其包含50至80重量%的丙烯均聚物和10至70重量%的丙烯共聚物,其具有5至50重量%的C 2 其中聚合成与丙烯不同的烷基-1-烯,并且可以通过采用齐格勒 - 纳塔催化剂体系的两步聚合由气相获得 。 在第一聚合步骤中,丙烯在10至50巴的压力,50至100℃的温度和在至少2.0%的存在下反应混合物的平均停留时间为0.3至5小时的聚合反应, ,基于总体积的氢气。 将所述第一聚合步骤中获得的丙烯均聚物与齐格勒 - 纳塔催化剂体系一起转移到中间容器中,膨胀0.01至5分钟至小于5巴,并保持在10至80℃的温度。 然后通过在压力下引入气体混合物将中间容器增加5至60巴,然后将丙烯均聚物与齐格勒 - 纳塔催化剂体系一起转移到第二聚合步骤。 在所述第二聚合步骤中,将丙烯和C 12 -C 13烷-1-烯的混合物在10至50巴的压力下聚合成丙烯均聚物 ,温度为50〜100℃,平均停留时间为0.5〜5小时。 在第一聚合步骤中反应的单体和在第二聚合步骤中反应的单体之间的重量比被调节至4:1至1:1的范围内。
    • 3. 发明授权
    • Impact resistant polyolefin compositions
    • 耐冲击聚烯烃组合物
    • US07482406B2
    • 2009-01-27
    • US10551682
    • 2004-03-29
    • Jean NewsPaola MassariHans-Jürgen Zimmermann
    • Jean NewsPaola MassariHans-Jürgen Zimmermann
    • C08L23/14C08F297/08C08F4/649
    • C08F10/00C08F210/16C08L23/0815C08L23/10C08L23/16Y10S526/905C08F4/651C08L2666/06C08F210/06C08F2500/12C08F2500/17C08F2500/04
    • Olefin polymer composition comprising (by weight, unless otherwise specified): A) 60-95% of a propylene homopolymer or copoloymer having a Polydispersity Index (P.I.) value of from 4.6 to 10 and a content of isotactic pentads (mmmm), measured by 13C NMR on the fraction insoluble in xylene at 25° C., higher than 98 molar, B) 5-40% of a copolymer of ethylene containing from 40% to 70% of propylene or C4-C10 α-olefins) or of combinations thereof, and optionally minor proportions of a diene; said composition having a Temperature Rising Elution Fractionation (TREF) profile, obtained by fractionation in xylene and collection of fractions at temperatures of 40° C., 80° C. and 90° C., in which the ethylene content Y of the fraction collected at 90° C. satisfies the following relation (1): Y≦−0.8+0.035X+0.0091X2 wherein X is the ethylene content of the fraction collected at 40° C. and both X and Y are expressed in percent by weight, and a value of intrinsic viscosity [η] of the fraction soluble in xylene at 25° C. of from 1.8 to 4.2 dl/g.
    • 烯烃聚合物组合物包含(按重量计,除非另有说明):A)60-95%的多分散指数(PI)值为4.6至10的丙烯均聚物或共聚合物和全同立构五单元组(mmmm)的含量,通过 在25℃,高于98摩尔的不溶于二甲苯的级分上的13C NMR,B)5-40%含有40%至70%丙烯或C 4 -C 10α-烯烃的乙烯共聚物)或组合 和任选地较小比例的二烯; 所述组合物具有通过在二甲苯中分馏并在40℃,80℃和90℃的温度下收集馏分获得的升温洗脱分馏(TREF)分布,其中收集馏分的乙烯含量Y 满足以下关系式(1):Y <= -0.8 + 0.035X + 0.0091X2其中X是在40℃收集的馏分的乙烯含量,X和Y都以重量百分比表示 ,在25℃下可溶于二甲苯的馏分的特性粘度η值为1.8-4.2dl / g。