Poly(phenylene ether) process
    1.
    发明授权
    Poly(phenylene ether) process 有权
    聚(苯醚)工艺

    公开(公告)号:US08466253B1

    公开(公告)日:2013-06-18

    申请号:US13538020

    申请日:2012-06-29

    IPC分类号: C08G64/00 C08G63/02

    摘要: A method of purifying a capped poly(phenylene ether) includes mixing a poly(phenylene ether) capping reaction mixture comprising a capped poly(phenylene ether), a capping agent, a capping byproduct, a capping catalyst, and a poly(phenylene ether) solvent, and first washing solvents comprising a C1-C4 alkanol and water to form a first liquid phase comprising the capped poly(phenylene ether) and poly(phenylene ether) solvent, and a second liquid phase comprising C1-C4 alkanol and water; and separating the first liquid phase from the second liquid phase. Capped poly(phenylene ether) having reduced levels of residual capping agent, capping byproduct, and capping catalyst is produced from poly(phenylene ether) capping reaction mixtures by this method.

    摘要翻译: 一种纯化封端聚(亚苯基醚)的方法包括混合包含封端的聚(苯醚),封端剂,封端副产物,封端催化剂和聚苯醚的聚(苯醚)封端反应混合物, 溶剂和包含C1-C4链烷醇和水的第一洗涤溶剂以形成包含封端的聚(苯醚)和聚(苯醚)溶剂的第一液相,以及包含C 1 -C 4烷醇和水的第二液相; 以及将第一液相与第二液相分离。 通过该方法由聚(苯醚)封端反应混合物产生具有降低的残余封端剂,封端副产物和封端催化剂水平的封端的聚苯醚。

    POLY(PHENYLENE ETHER) PROCESS
    2.
    发明申请
    POLY(PHENYLENE ETHER) PROCESS 有权
    聚(苯乙烯)工艺

    公开(公告)号:US20130225783A1

    公开(公告)日:2013-08-29

    申请号:US13417451

    申请日:2012-03-12

    IPC分类号: C08G65/46

    CPC分类号: C08G65/46

    摘要: A method of purifying a poly(phenylene ether) is described. The method includes mixing a poly(phenylene ether) solution comprising a poly(phenylene ether) and a poly(phenylene ether) solvent with first washing solvents including a C1-C4 alkanol and water to form a first liquid phase including poly(phenylene ether) and poly(phenylene ether) solvent, and a second liquid phase comprising C1-C4 alkanol and water, and separating the first liquid phase from the second liquid phase. The first and second liquid phases combined comprise about 60 to about 95 weight percent poly(phenylene ether) solvent, about 4 to about 32 weight percent C1-C4 alkanol, and about 1 to about 36 weight percent water. When optionally combined with evaporative removal of the poly(phenylene ether) solvent, the method reduces C1-C4 alkanol usage compared to the antisolvent precipitation method, and it produces poly(phenylene ether) having reduced catalyst metal ion residue and reduced color.

    摘要翻译: 描述了一种纯化聚(苯醚)的方法。 该方法包括将包含聚(苯醚)和聚(苯醚)溶剂的聚(苯醚)溶液与包含C1-C4链烷醇和水的第一洗涤溶剂混合以形成包含聚(苯醚) 和聚(苯醚)溶剂,以及包含C 1 -C 4链烷醇和水的第二液相,并且将第一液相与第二液相分离。 组合的第一和第二液相包含约60至约95重量%的聚(苯醚)溶剂,约4至约32重量%的C 1 -C 4链烷醇和约1至约36重量%的水。 当与蒸馏除去聚(苯醚)溶剂相结合时,与反溶剂沉淀法相比,该方法降低了C1-C4链烷醇的用量,并且产生具有降低的催化剂金属离子残余物和降低颜色的聚苯醚。

    Poly(phenylene ether) process
    3.
    发明授权
    Poly(phenylene ether) process 有权
    聚(苯醚)工艺

    公开(公告)号:US08859646B2

    公开(公告)日:2014-10-14

    申请号:US13417451

    申请日:2012-03-12

    IPC分类号: C08F6/08 C08G65/38

    CPC分类号: C08G65/46

    摘要: A method of purifying a poly(phenylene ether) is described. The method includes mixing a poly(phenylene ether) solution comprising a poly(phenylene ether) and a poly(phenylene ether) solvent with first washing solvents including a C1-C4 alkanol and water to form a first liquid phase including poly(phenylene ether) and poly(phenylene ether) solvent, and a second liquid phase comprising C1-C4 alkanol and water, and separating the first liquid phase from the second liquid phase. The first and second liquid phases combined comprise about 60 to about 95 weight percent poly(phenylene ether) solvent, about 4 to about 32 weight percent C1-C4 alkanol, and about 1 to about 36 weight percent water. When optionally combined with evaporative removal of the poly(phenylene ether) solvent, the method reduces C1-C4 alkanol usage compared to the antisolvent precipitation method, and it produces poly(phenylene ether) having reduced catalyst metal ion residue and reduced color.

    摘要翻译: 描述了一种纯化聚(苯醚)的方法。 该方法包括将包含聚(苯醚)和聚(苯醚)溶剂的聚(苯醚)溶液与包含C1-C4链烷醇和水的第一洗涤溶剂混合以形成包含聚(苯醚) 和聚(苯醚)溶剂,以及包含C 1 -C 4链烷醇和水的第二液相,并且将第一液相与第二液相分离。 组合的第一和第二液相包含约60至约95重量%的聚(苯醚)溶剂,约4至约32重量%的C 1 -C 4链烷醇和约1至约36重量%的水。 当与蒸馏除去聚(苯醚)溶剂相结合时,与反溶剂沉淀法相比,该方法降低了C1-C4链烷醇的用量,并且产生具有降低的催化剂金属离子残余物和降低颜色的聚苯醚。

    POLY(PHENYLENE ETHER) COPOLYMER AND METHOD OF MAKING
    4.
    发明申请
    POLY(PHENYLENE ETHER) COPOLYMER AND METHOD OF MAKING 有权
    聚(苯乙烯)共聚物及其制备方法

    公开(公告)号:US20150038667A1

    公开(公告)日:2015-02-05

    申请号:US13881480

    申请日:2012-07-27

    IPC分类号: C08G65/44 C08G65/46

    摘要: A poly(phenylene ether) copolymer comprising about 5 to 40 mole percent repeat units derived from 2-phenylphenol and 60 to about 95 mole percent repeat units derived from 2,6-dimethylphenol, wherein the poly(phenylene ether) copolymer has a weight average molecular weight of at least 8,000 atomic mass units, is disclosed. Also disclosed is a method of preparing the poly(phenylene ether) copolymer, the method comprising oxidatively copolymerizing a monomer mixture comprising about 5 to 40 mole percent 2-phenylphenol and about 60 to about 95 mole percent 2,6-dimethylphenol in the presence of a solvent, molecular oxygen, and a polymerization catalyst comprising a metal ion and at least one amine ligand to form a solution of the poly(phenylene ether) copolymer in the solvent, wherein a ratio of total moles of 2-phenylphenol and 2,6-dimethylphenol to moles of metal ion is about 10:1 to about 1200:1.

    摘要翻译: 包含约5-40摩尔%的衍生自2-苯基苯酚的重复单元和衍生自2,6-二甲基苯酚的重均分子量为60-约95摩尔%的聚(苯醚)共聚物,其中聚苯醚共聚物具有重均分子量 分子量至少为8,000原子质量单位。 还公开了制备聚(苯醚)共聚物的方法,该方法包括在包含约5至40摩尔%的2-苯基苯酚和约60至约95摩尔%2,6-二甲基苯酚的单体混合物的存在下, 溶剂,分子氧和包含金属离子和至少一种胺配体的聚合催化剂,以在溶剂中形成聚(苯醚)共聚物的溶液,其中2-苯基苯酚和2,6-二羟基苯酚的总摩尔比 二甲基酚与金属离子的摩尔数为约10:1至约1200:1。

    Poly(phenylene ether) copolymer and method of making
    5.
    发明授权
    Poly(phenylene ether) copolymer and method of making 有权
    聚(苯醚)共聚物及其制备方法

    公开(公告)号:US09018342B2

    公开(公告)日:2015-04-28

    申请号:US13881480

    申请日:2012-07-27

    摘要: A poly(phenylene ether) copolymer comprises about 5 to 40 mole percent repeat units derived from 2-phenylphenol and 60 to about 95 mole percent repeat units derived from 2,6-dimethylphenol, wherein the poly(phenylene ether) copolymer has a weight average molecular weight of at least 8,000 atomic mass units, as measured by gel permeation chromatography. A method of preparing the poly(phenylene ether) copolymer, comprises oxidatively copolymerizing a monomer mixture comprising about 5 to 40 mole percent 2-phenylphenol and about 60 to about 95 mole percent 2,6-dimethylphenol in the presence of a solvent, molecular oxygen, and a polymerization catalyst comprising a metal ion and at least one amine ligand to form a solution of the poly(phenylene ether) copolymer in the solvent, wherein a ratio of total moles of 2-phenylphenol and 2,6-dimethylphenol to moles of metal ion is about 10:1 to about 1200:1.

    摘要翻译: 聚(苯醚)共聚物包含约5-40摩尔%的衍生自2-苯基苯酚的重复单元和60-约95摩尔%的衍生自2,6-二甲基苯酚的重复单元,其中聚(苯醚)共聚物具有重均分子量 通过凝胶渗透色谱法测量的至少8,000个原子质量单位的分子量。 制备聚(苯醚)共聚物的方法包括在溶剂存在下氧化共聚包含约5至40摩尔%的2-苯基苯酚和约60至约95摩尔%的2,6-二甲基苯酚的单体混合物,分子氧 ,以及包含金属离子和至少一种胺配体的聚合催化剂,以在溶剂中形成聚(苯醚)共聚物的溶液,其中2-苯基苯酚和2,6-二甲基苯酚的总摩尔数与摩尔数 金属离子为约10:1至约1200:1。

    RUBBER COMPOSITION, METHOD FOR ITS FORMATION, AND AUTOMOTIVE TIRE CONTAINING THE COMPOSITION
    6.
    发明申请
    RUBBER COMPOSITION, METHOD FOR ITS FORMATION, AND AUTOMOTIVE TIRE CONTAINING THE COMPOSITION 有权
    橡胶组合物,其形成方法和含有组合物的汽车轮胎

    公开(公告)号:US20140011926A1

    公开(公告)日:2014-01-09

    申请号:US14010959

    申请日:2013-08-27

    IPC分类号: C08L71/12 C08K5/523 C08K5/01

    摘要: A rubber composition with disperse phase particles containing poly(phenylene ether) can be formed by a method that includes melt blending an uncured rubber with a poly(phenylene ether) composition containing a poly(phenylene ether) and an oil to form an uncured rubber composition, then curing the uncured rubber composition. Before being blended with the rubber, the poly(phenylene ether) composition exhibits a glass transition temperature of about 40 to about 140° C., and during blending with the rubber, the oil component of poly(phenylene ether) composition migrates from the poly(phenylene ether) composition to the rubber, leaving a poly(phenylene ether)-containing disperse phase that gives rise to a second hysteresis peak temperature of about 160 to about 220° C. as measured by dynamic mechanical analysis of the cured rubber composition. Also described are the poly(phenylene ether) composition used in the method, a cured rubber composition formed by the method, and a tire containing the cured rubber composition.

    摘要翻译: 含有聚(苯醚)的分散相颗粒的橡胶组合物可以通过包括将未固化的橡胶与含有聚(苯醚)和油的聚(苯醚)组合物熔融共混以形成未固化的橡胶组合物的方法形成 ,然后固化未固化的橡胶组合物。 在与橡胶混合之前,聚(苯醚)组合物的玻璃化转变温度为约40至约140℃,并且在与橡胶共混期间,聚(苯醚)组合物的油组分从聚 (亚苯基醚)组合物与橡胶反应,留下含聚亚苯基醚的分散相,其通过固化的橡胶组合物的动态机械分析测量,产生约160至约220℃的第二滞后峰值温度。 还描述了该方法中使用的聚(苯醚)组合物,通过该方法形成的固化橡胶组合物和含有固化橡胶组合物的轮胎。

    Rubber composition, method for its formation, and automotive tire containing the composition
    10.
    发明授权
    Rubber composition, method for its formation, and automotive tire containing the composition 有权
    橡胶组合物,其形成方法和含有组合物的汽车轮胎

    公开(公告)号:US08557937B1

    公开(公告)日:2013-10-15

    申请号:US13488701

    申请日:2012-06-05

    摘要: A rubber composition with disperse phase particles containing poly(phenylene ether) can be formed by a method that includes melt blending an uncured rubber with a poly(phenylene ether) composition containing a poly(phenylene ether) and an oil to form an uncured rubber composition, then curing the uncured rubber composition. Before being blended with the rubber, the poly(phenylene ether) composition exhibits a glass transition temperature of about 40 to about 140° C., and during blending with the rubber, the oil component of poly(phenylene ether) composition migrates from the poly(phenylene ether) composition to the rubber, leaving a poly(phenylene ether)-containing disperse phase that gives rise to a second hysteresis peak temperature of about 160 to about 220° C. as measured by dynamic mechanical analysis of the cured rubber composition. Also described are the poly(phenylene ether) composition used in the method, a cured rubber composition formed by the method, and a tire containing the cured rubber composition.

    摘要翻译: 含有聚(苯醚)的分散相颗粒的橡胶组合物可以通过包括将未固化的橡胶与含有聚(苯醚)和油的聚(苯醚)组合物熔融共混以形成未固化的橡胶组合物的方法形成 ,然后固化未固化的橡胶组合物。 在与橡胶混合之前,聚(苯醚)组合物的玻璃化转变温度为约40至约140℃,并且在与橡胶共混期间,聚(苯醚)组合物的油组分从聚 (亚苯基醚)组合物与橡胶反应,留下含聚亚苯基醚的分散相,其通过固化的橡胶组合物的动态机械分析测量,产生约160至约220℃的第二滞后峰值温度。 还描述了该方法中使用的聚(苯醚)组合物,通过该方法形成的固化橡胶组合物和含有固化橡胶组合物的轮胎。