MULTI-COMPONENT CATALYST SYSTEMS AND POLYMERIZATION PROCESSES FOR FORMING IN-SITU HETEROPHASIC COPOLYMERS AND/OR VARYING THE XYLENE SOLUBLES CONTENT OF POLYOLEFINS
    91.
    发明申请
    MULTI-COMPONENT CATALYST SYSTEMS AND POLYMERIZATION PROCESSES FOR FORMING IN-SITU HETEROPHASIC COPOLYMERS AND/OR VARYING THE XYLENE SOLUBLES CONTENT OF POLYOLEFINS 有权
    多组分催化剂体系和形成异源共聚物的聚合方法和/或改变聚烯烃的二甲苯溶液含量

    公开(公告)号:US20110269923A1

    公开(公告)日:2011-11-03

    申请号:US13180672

    申请日:2011-07-12

    Abstract: Embodiments of the invention generally include multi-component catalyst systems, polymerization processes and heterophasic copolymers formed by the processes. The multi-component catalyst system generally includes a first catalyst component selected from Ziegler-Natta catalyst systems including a diether internal electron donor and a metallocene catalyst represented by the general formula XCpACpBMAn, wherein X is a structural bridge, CpA and CpB each denote a cyclopentadienyl group or derivatives thereof, each being the same or different and which may be either substituted or unsubstituted, M is a transition metal and A is an alkyl, hydrocarbyl or halogen group and n is an integer between 0 and 4. The multi-component catalyst system further includes a second catalyst component generally represented by the formula XCpACpBMAn, wherein X is a structural bridge, CpA and CpB each denote a cyclopentadienyl group or derivatives thereof, each being the same or different and which may be either substituted or unsubstituted, M is a transition metal and A is an alkyl, hydrocarbyl or halogen group and n is an integer between 0 and 4 and wherein the second catalyst component exhibits a higher ethylene response than the first catalyst component.

    Abstract translation: 本发明的实施方案通常包括通过该方法形成的多组分催化剂体系,聚合方法和多相共聚物。 多组分催化剂体系通常包括选自齐格勒 - 纳塔催化剂体系的第一催化剂组分,其包括二醚内电子给体和由通式XCpACpBMAn表示的茂金属催化剂,其中X是结构桥,CpA和CpB各自表示环戊二烯基 基团或其衍生物,各自相同或不同,并且可以是取代或未取代的,M是过渡金属,A是烷基,烃基或卤素基团,n是0和4之间的整数。多组分催化剂 系统还包括通常由式XCpACpBMAn表示的第二催化剂组分,其中X是结构桥,CpA和CpB各自表示环戊二烯基或其衍生物,各自相同或不同,并且可以是取代或未取代的,M是 过渡金属,A是烷基,烃基或卤素基团,n是0至4之间的整数, nd催化剂组分表现出比第一催化剂组分更高的乙烯响应。

    Methods for Production of High Impact Polystyrene
    95.
    发明申请
    Methods for Production of High Impact Polystyrene 审中-公开
    高抗冲聚苯乙烯生产方法

    公开(公告)号:US20110201757A1

    公开(公告)日:2011-08-18

    申请号:US13093160

    申请日:2011-04-25

    CPC classification number: C08F279/02

    Abstract: A method of preparing a high impact polystyrene comprising contacting styrene monomer, a high cis polybutadiene elastomer, and an initiator under high shear within a reaction zone. A high-impact polystyrene comprising a high cis polybutadiene elastomer. A method of preparing a high impact polystyrene comprising contacting styrene monomer, a high cis polybutadiene elastomer, and an initiator under extreme reaction conditions within a reaction zone.

    Abstract translation: 一种制备高抗冲聚苯乙烯的方法,包括在反应区内高剪切下使苯乙烯单体,高顺式聚丁二烯弹性体和引发剂接触。 包含高顺式聚丁二烯弹性体的高抗冲聚苯乙烯。 一种制备高抗冲聚苯乙烯的方法,包括在反应区内的极端反应条件下使苯乙烯单体,高顺式聚丁二烯弹性体和引发剂接触。

    Dilute Liquid Phase Alkylation
    97.
    发明申请
    Dilute Liquid Phase Alkylation 有权
    稀液相烷基化

    公开(公告)号:US20110130609A1

    公开(公告)日:2011-06-02

    申请号:US13024602

    申请日:2011-02-10

    Inventor: James R. Butler

    Abstract: Methods of forming ethylbenzene are described herein. In one embodiment, the method includes contacting dilute ethylene with benzene in the presence of an alkylation catalyst to form ethylbenzene, wherein such contact occurs in a liquid phase reaction zone and recovering ethylbenzene from the reaction zone.

    Abstract translation: 本文描述了形成乙苯的方法。 在一个实施方案中,该方法包括在烷基化催化剂存在下使稀乙烯与苯接触以形成乙苯,其中这种接触发生在液相反应区中并从反应区回收乙苯。

    Blends of polypropylene impact copolymers with other polymers
    99.
    发明授权
    Blends of polypropylene impact copolymers with other polymers 有权
    聚丙烯抗冲共聚物与其他聚合物的共混物

    公开(公告)号:US07892475B2

    公开(公告)日:2011-02-22

    申请号:US12246709

    申请日:2008-10-07

    Abstract: It has been discovered that the properties of sheet or film materials of broad molecular weight distribution ethylene/propylene rubber impact-modified heterophasic copolymer (ICP) can be improved by blending the ICP with a second polyolefin. The second polyolefin may be a syndiotactic polypropylene (sPP), a random copolymer (RCP) of propylene and comonomer (e.g. ethylene and/or butene) made using a Ziegler-Natta or metallocene catalyst, medium density polyethylene (MDPE), linear low density polyethylene (LLDPE), or low crystalline copolymer of propylene/α-olefin. Improvements include, but are not necessarily limited to, reduced motor amps, lower secant modulus, increased dart drop strength, increased gloss, reduced haze, increased elongation to yield, elimination of stress whitening, improved puncture resistance, and decreased seal initiation temperature. This sheet of film materials may be co-extruded with other resins or laminated with other materials after extrusion.

    Abstract translation: 已经发现,通过将ICP与第二聚烯烃共混可以提高宽分子量分布乙烯/丙烯橡胶冲击改性多相共聚物(ICP)的片材或薄膜材料的性能。 第二聚烯烃可以是间同立构聚丙烯(sPP),使用齐格勒 - 纳塔或茂金属催化剂制备的丙烯和共聚单体(例如乙烯和/或丁烯)的无规共聚物(RCP),中密度聚乙烯(MDPE),线性低密度 聚乙烯(LLDPE)或丙烯/α-烯烃的低结晶共聚物。 改进包括但不限于减少的电动机放大器,较低的正割模量,较高的飞镖下落强度,增加的光泽度,降低的雾度,增加的屈服伸长率,消除应力增白,改进的抗穿刺性和降低的密封起始温度。 这片薄膜材料可以与其它树脂共挤出,或者在挤压后与其它材料层压。

    Process for the Oxidative Coupling of Methane
    100.
    发明申请
    Process for the Oxidative Coupling of Methane 有权
    甲烷氧化偶合过程

    公开(公告)号:US20100331595A1

    公开(公告)日:2010-12-30

    申请号:US12494117

    申请日:2009-06-29

    Abstract: A method for the oxidative coupling of hydrocarbons, such as the oxidative coupling of methane, includes providing an oxidative catalyst inside a reactor, and carrying out the oxidative coupling reaction under a set of reaction conditions. The oxidative catalyst includes (A) at least one element selected from the group consisting of the Lanthanoid group, Mg, Ca, and the elements of Group 4 of the periodic table (Ti, Zr, and Hf); (B) at least one element selected from the group consisting of the Group 1 elements of Li, Na, K, Rb, Cs, and the elements of Group 3 (including La and Ac) and Groups 5-15 of the periodic table; (C) at least one element selected from the group consisting of the Group 1 elements of Li, Na, K, Rb, Cs, and the elements Ca, Sr, and Ba; and (D) oxygen.

    Abstract translation: 烃的氧化偶合的方法,例如甲烷的氧化偶联,包括在反应器内提供氧化催化剂,并在一组反应条件下进行氧化偶联反应。 氧化催化剂包括(A)选自镧系元素,Mg,Ca和元素周期表第4族元素(Ti,Zr和Hf)中的至少一种元素; (B)选自Li,Na,K,Rb,Cs的第1族元素和第3族元素(包括La和Ac)和元素周期表第5-15族中的至少一种元素; (C)选自Li,Na,K,Rb,Cs族元素和元素Ca,Sr和Ba中的至少一种元素; 和(D)氧气。

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