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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。
    • 5. 发明授权
    • Propylene polymers
    • 丙烯聚合物
    • US06495634B2
    • 2002-12-17
    • US09097865
    • 1998-06-16
    • Stephan HüfferJoachim RöschFranz LanghauserDieter LilgeRoland Hingmann
    • Stephan HüfferJoachim RöschFranz LanghauserDieter LilgeRoland Hingmann
    • C08L2312
    • C08L23/10C08F10/06C08F210/16C08L23/14C08L23/142C08L2205/02C08F2/001C08F4/025C08F4/651C08F4/6546C08L2666/04C08F210/06C08F2500/12
    • Propylene polymers containing a matrix of a propylene homopolymer and a copolymer of propylene and other alkenes, wherein, during the separation of the propylene polymers according to tacticity and comonomer distribution of the polymer chains, by first dissolving the propylene polymers in boiling xylene, then cooling the solution at a cooling rate of 10° C./h to 25° C. and thereafter, increasing the temperature, separating the propylene polymers into fractions of different solubility, either one or more of the conditions that i) more than 20% by weight of the matrix remain undissolved on further heating to 112° C. or ii) more than 8% by weight of the matrix remain undissolved on further heating to 117° C. or iii) more than 1% by weight of the matrix remain undissolved on further heating to 122° C. are fulfilled by the matrix which remains undissolved on heating the cooled propylene polymer solution to 80° C., a process for the preparation of the propylene polymers, their use for the production of films, fibers or moldings and the films, fibers or moldings comprising these propylene polymers, are described.
    • 含有丙烯均聚物基质和丙烯与其它烯烃共聚物的丙烯聚合物,其中在根据聚合物链的立构规整度和共聚单体分布分离丙烯聚合物期间,首先将丙烯聚合物溶解在沸腾的二甲苯中,然后冷却 该溶液以10℃/ h至25℃的冷却速率,然后升高温度,将丙烯聚合物分离成不同溶解度的分数,其中的一种或多种条件为:超过20重量% 的基质在进一步加热至112°C时仍未溶解。或)在基于进一步加热至117℃时,基质重量不得超过8%。或者,更多加热时,大于1重量%的基质仍然不溶解 至122℃,通过在将冷却的丙烯聚合物溶液加热至80℃时仍未溶解的基质来实现,制备丙烯聚合物的方法,其用于p 描述了膜,纤维或模制品的引导以及包含这些丙烯聚合物的膜,纤维或模制品。
    • 7. 发明授权
    • Water-dilutable binders, aqueous paints containing these binders, and process for priming or painting plastics materials with a single coat of paint
    • US06191210B1
    • 2001-02-20
    • US09043559
    • 1998-06-23
    • Joachim RöschHarald BorgholteHorst Hintze-Brüning
    • Joachim RöschHarald BorgholteHorst Hintze-Brüning
    • C08L3100
    • C09D151/06
    • The invention relates to water-dilutable binders which can be prepared by subjecting (A) from 20 to 90% by weight of a mixture of (a1) from 3 to 50% by weight of acrylic acid, methacrylic acid or of a mixture of acrylic acid and methacrylic acid, and (a2) from 50 to 97% by weight of an ethylenically unsaturated monomer or of a mixture of ethylenically unsaturated monomers to free-radical polymerization in the presence of (B) from 9.9 to 79.9% by weight of a halogen-free copolymer composed of (b1) from 1 to 99, preferably from 50 to 90% by weight, of propylene, (b2) from 1 to 99, preferably from 10 to 50% by weight, of at least one olefin which is copolymerizable with (b1) and contains per molecule from five to twenty, preferably from six to eight, carbon atoms, with the exception of isoprene, and (b3) from 0 to 50, preferably from 0 to 25% by weight, of ethylene and/or butylene, or of a mixture of such copolymers, and (C) from 0.1 to 10% by weight of a free-radical initiator or of a mixture of free-radical initiators, and, after neutralization of at least 20% of the carboxyl groups which are present in the resulting polymerization product, dispersing the polymerization product in water, the sum of the percentages by weight of components (A), (B) and (C) and of (a1) and (a2) being in each case always 100% by weight, and the composition of the mixture of (al) and (a2) being selected such that polymerization of the mixture of (al) and (a2) alone gives a polymer which has a glass transition temperature of from 0 to 150° C., and contains from 0.04 to 1.0 milliequivalent of one or more of the following functional groups: —COOH, —OH, —NR3, —CN, —CONH2, —CO—, —NHCONH—, —OCONH—, —OP3H, —OSO3H, —R—O—R—, where R is an organic radical.