会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 2. 发明申请
    • POLYETHYLENE COMPOSITIONS, METHODS OF MAKING THE SAME, AND ARTICLES PREPARED THEREFROM
    • 聚乙烯组合物,其制备方法和制备的制品
    • WO2008051824A2
    • 2008-05-02
    • PCT/US2007/081893
    • 2007-10-19
    • DOW GLOBAL TECHNOLOGIES INC.MICHIE, WilliamCHANG, DaneHAZLITT, LonnieWHITED, StephanieKINNAN, MichaelNEUBAUER, AnthonyHO, Thoi
    • MICHIE, WilliamCHANG, DaneHAZLITT, LonnieWHITED, StephanieKINNAN, MichaelNEUBAUER, AnthonyHO, Thoi
    • C08L23/00
    • C08L23/26C08L23/0815C08L2205/02C08L2666/06
    • The invention is related to compositions suitable for the fabrication of pipes, and other articles, with excellent performance properties. The invention provides a composition, comprising a blend, wherein said blend comprises a high molecular weight ethylene-based interpolymer and a low molecular weight ethylene-based interpolymer, and the high molecular weight ethylene-based interpolymer is a heterogeneously branched linear or a homogeneously branched linear ethylene-based interpolymer, and has a density from 0.922 g/cc to 0.929 g/cc, and a high load melt index (I21) from 0.2 g/10 min to 1.0 g/10 min, and the low molecular weight ethylene-based interpolymer is heterogeneously branched linear or a homogeneously branched linear ethylene-based interpolymer, and has a density from 0.940 g/cc to 0.955 g/cc, and a melt index (I2) from 6 g/10 min to 50 g/10 min. The blend has a single peak in an ATREF profile eluting above 30°C, and has a coefficient of viscosity average molecular weight (CM?) less than -0.0032 in the log(calculated Mv) versus elution temperature, said CMv calculated in the range of elution temperatures from 70°C to 90°C. The Mv is the viscosity average molecular weight.
    • 本发明涉及适于制造具有优异性能的管道和其它制品的组合物。 本发明提供一种包含共混物的组合物,其中所述共混物包含高分子量乙烯基互聚物和低分子量乙烯基互聚物,并且高分子量乙烯基互聚物是非均匀支化的线性或均匀分支的 线性乙烯类互聚物,密度为0.922g / cc〜0.929g / cc,高负荷熔融指数(I21)为0.2g / 10min〜1.0g / 10min,低分子量乙烯 - 基于异构支化的线型或均匀支化的线性乙烯基互聚物,其密度为0.940g / cc至0.955g / cc,熔体指数(I 2)为6g / 10min至50g / 10min 。 共混物在高于30℃洗脱的ATREF谱中具有单峰,并且在对数(计算出的Mv)相对于洗脱温度具有小于-0.0032的粘均分子量(CMΩ)系数,所述CMv计算在范围内 的洗脱温度为70℃至90℃。 Mv是粘均分子量。
    • 4. 发明申请
    • PROCESS FOR PRODUCING HIGH QUALITY IONOMERS
    • 生产高质量离聚体的方法
    • WO2008057979A2
    • 2008-05-15
    • PCT/US2007/083407
    • 2007-11-02
    • DOW GLOBAL TECHNOLOGIES INC.WALTHER, BrianNEUBAUER, AnthonyKIM, EungPAVLICEK, CalvinDIEHL, Charles
    • WALTHER, BrianNEUBAUER, AnthonyKIM, EungPAVLICEK, CalvinDIEHL, Charles
    • C08F8/44
    • C08F8/44B29C47/6025B29C47/6031B29C47/6037B29C47/6056C08F210/02C08F2800/20C08F8/12C08F220/06
    • A reactive extrusion process for producing an ionomer is disclosed. The process comprising adding a polymer containing a carboxyl functionality to an extruder, then homogenously melting the polymer in a melting zone of the extruder. A first melt seal zone of the extruder is formed to separate the melting zone from an injection zone where an aqueous solution of metallic ions are added to the molten polymer. The first melt seal zone is formed by increasing the pressure in the melt seal zone to a pressure which is higher than the vapor pressure of the water at any point in the injection zone and the reaction zone. The aqueous solution of metallic ions is then mixed with the polymer containing the carboxyl functionality in a reaction zone of the extruder under conditions such that the metallic ions are substantially reacted with the carboxyl functionality. A pressure build-up zone is formed in the extruder, wherein the pressure build-up zone is located no earlier than at the end of the reaction zone wherein the pressure build-up zone is formed by increasing the pressure to a level such that the aqueous solution of metallic ions remains in the liquid phase for a time sufficient to allow for the desired reaction between the metallic ions and the carboxyl functionality of the polymer.
    • 公开了一种用于生产离聚物的反应性挤出方法。 该方法包括将含有羧基官能团的聚合物加入到挤出机中,然后在挤出机的熔融区中均匀熔融聚合物。 形成挤出机的第一熔融密封区域以将熔融区与注入区分离,在注入区中金属离子的水溶液被添加到熔融聚合物中。 第一熔体密封区域通过将熔体密封区域中的压力增加至高于注入区域和反应区域中的任何点处的水蒸气压力的压力而形成。 然后在金属离子基本上与羧基官能团反应的条件下,在挤出机的反应区中将金属离子的水溶液与含有羧基官能团的聚合物混合。 在挤出机中形成压力形成区,其中压力形成区的位置不早于在反应区的末端,其中压力形成区通过将压力增加至使得 金属离子的水溶液在液相中保持足够的时间以允许金属离子与聚合物的羧基官能团之间的所需反应。