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    • 2. 发明申请
    • ZIEGLER-NATTA CATALYST COMPOSITION WITH CONTROLLED MORPHOLOGY
    • ZIEGLER-NATTA催化剂组合物与控制形态
    • US20120202955A1
    • 2012-08-09
    • US13022021
    • 2011-02-07
    • LEI ZHANGKenneth BlackmonDavid Rauscher
    • LEI ZHANGKenneth BlackmonDavid Rauscher
    • C08F4/60
    • C08F10/00C08F110/02C08F4/6557C08F2500/04C08F2500/11C08F2500/12C08F2500/17C08F2500/18C08F2500/20C08F2500/23C08F2500/26
    • Catalyst Systems, processes of forming the same and polymers and polymerization processes are described herein. The process of forming the catalyst system generally includes providing a first compound including a magnesium dialkoxide and aluminum alkoxide: contacting the first compound with a first agent and a second agent to form a solution of reaction product “A”, the first agent including a titanating agent and the second agent including a first metal halide; contacting the solution of reaction product “A” with a third agent to form a solid reaction product “B”, the third agent including a second metal halide: contacting the solid reaction product “B” with a fourth agent to form a solid reaction product “C”, the fourth agent including a third metal halide: optionally contacting the solid reaction product “C” with a fifth agent to form a solid reaction product “D”, the fifth agent including a fourth metal halide; and contacting the solid reaction product “C” or “D” with a sixth agent to form a catalyst component, the sixth agent including a first organoaluminum compound.
    • 催化剂体系,其形成方法,聚合物和聚合方法在本文中描述。 形成催化剂体系的方法通常包括提供包含二烷氧基镁和烷氧化铝的第一化合物:使第一化合物与第一试剂和第二试剂接触以形成反应产物“A”的溶液,第一试剂包括滴定 试剂和第二试剂包括第一金属卤化物; 使反应产物“A”的溶液与第三试剂接触以形成固体反应产物“B”,第三试剂包括第二金属卤化物:使固体反应产物“B”与第四试剂接触以形成固体反应产物 “C”,第四剂包括第三金属卤化物:任选地使固体反应产物“C”与第五试剂接触以形成固体反应产物“D”,第五试剂包括第四金属卤化物; 并使固体反应产物“C”或“D”与第六试剂接触以形成催化剂组分,第六试剂包括第一有机铝化合物。
    • 6. 发明申请
    • Sequential Formation of Ziegler-Natta Catalyst Using Non-blended Components
    • 使用非混合组分的齐格勒 - 纳塔催化剂的顺序形成
    • US20120046429A1
    • 2012-02-23
    • US12861349
    • 2010-08-23
    • Lei ZhangKenneth BlackmonDavid Rauscher
    • Lei ZhangKenneth BlackmonDavid Rauscher
    • C08F4/654C08F110/02B01J31/38
    • C08F10/00C08F110/02C08F4/6546C08F2500/04C08F2500/07C08F2500/12C08F2500/17C08F2500/18C08F2500/19C08F2500/20C08F2500/24C08F4/6557
    • Catalyst compositions, methods of forming the same and polymers formed therefrom are described herein. The methods of forming the catalysts generally include contacting an alkyl magnesium compound with a viscosity modifier prior to contact with an alcohol to form a magnesium dialkoxide compound; contacting the magnesium dialkoxide compound with a first titanium alkoxide and a first agent to form a first solution reaction product “A”, wherein the titanium alkoxide and the first agent are non-blended individual components prior to contacting the magnesium dialkoxide; contacting the first solution reaction product “A” with a second titanium alkoxide to form a second solution reaction product “B”; contacting the second solution reaction product “B” with a second agent to form a first solid reaction product “C”; contacting the first solid reaction product “C” with a third agent to form a second solid reaction product “D”; and contacting the second solid reaction product “D” with a reducing agent to limn a catalyst component.
    • 本文描述了催化剂组合物,其形成方法和由其形成的聚合物。 形成催化剂的方法通常包括在与醇接触之前使烷基镁化合物与粘度调节剂接触以形成二烷氧基镁化合物; 使二烷氧基镁化合物与第一钛醇盐和第一试剂接触以形成第一溶液反应产物“A”,其中在与二烷醇镁接触之前,所述钛醇盐和所述第一试剂是非混合的单独组分; 使第一溶液反应产物“A”与第二钛醇盐接触以形成第二溶液反应产物“B”; 使第二溶液反应产物“B”与第二试剂接触以形成第一固体反应产物“C”; 使第一固体反应产物“C”与第三试剂接触以形成第二固体反应产物“D”; 并使第二固体反应产物“D”与还原剂接触以使催化剂组分悬空。
    • 8. 发明申请
    • SYNTHESIS OF BRANCHED STYRENIC COPOLYMERS WITH P-T-BUTYLSTYRENE
    • 具有对叔丁基苯乙烯的分支苯乙烯共聚物的合成
    • US20050137373A1
    • 2005-06-23
    • US10742163
    • 2003-12-19
    • Jose SosaKenneth Blackmon
    • Jose SosaKenneth Blackmon
    • C08F212/04C08F212/12C08F212/34
    • C08F212/12C08F212/04
    • It has been discovered that improved polystyrene products may be obtained by polymerizing styrene in the presence of p-t-butyl styrene (TBS) and optionally at least one di-olefinic substituted aromatic compound, such as isopropenyl styrene, sec-butenyl styrene, m-isobutenyl styrene, p-diisopropenyl benzene, diallyl benzene, and/or diallyl phthalate. The resulting copolymers have a higher glass transition temperature (Tg), a higher molecular weight distribution (MWD), a higher Mz, and a lower melt flow index (MFI) as compared with a polymerized product made by an otherwise identical method except that TBS and/or the di-olefinic substituted aromatic compound are not used. These copolymers are also more highly branched as compared with a polymerized product made by an otherwise identical method in the absence of TBS and/or a di-olefinic substituted aromatic compound.
    • 已经发现,改性的聚苯乙烯产物可以通过在对叔丁基苯乙烯(TBS)和任选的至少一种二烯烃取代的芳族化合物如异丙烯基苯乙烯,仲丁烯基苯乙烯,间 - 异丁烯基 苯乙烯,对二异丙烯基苯,二烯丙基苯和/或邻苯二甲酸二烯丙酯。 与所制成的聚合产物相比,所得共聚物具有较高的玻璃化转变温度(T g),更高的分子量分布(MWD),更高的Mz和较低的熔体流动指数(MFI) 除了不使用TBS和/或二烯烃取代的芳族化合物之外,以相同的方法进行。 与在不存在TBS和/或二烯烃取代的芳族化合物的情况下通过相同的方法制备的聚合产物相比,这些共聚物也具有更高的支化度。