NOZZLE/HEADER DESIGN FOR POLYSTYRENE
    283.
    发明申请

    公开(公告)号:US20170282092A1

    公开(公告)日:2017-10-05

    申请号:US15085464

    申请日:2016-03-30

    CPC classification number: B01D1/007 B01D1/04 B01D1/06 B01D1/22 C08F6/005 C08L25/06

    Abstract: A vessel header includes lateral flow tubes arranged in a parallel configuration. The lateral flow tubes enter the vessel header through alternating vessel header penetrations with a single vessel header penetration per lateral flow tube. Each lateral flow tube has a perforated section within the vessel header having a non-circular cross-section having the shape of a circular sector, an elliptical sector, or an irregular quadrilateral. A method includes passing a molten polymer through the lateral flow tubes of the vessel header. The molten polymer exits the lateral flow tubes as strands through perforations in the lateral flow tubes within the vessel header. The method includes obtaining devolatilized polymer.

    Formation of a Ziegler-Natta catalyst

    公开(公告)号:US09650448B2

    公开(公告)日:2017-05-16

    申请号:US14304328

    申请日:2014-06-13

    CPC classification number: C08F4/6555 C08F10/00 C08F4/6557

    Abstract: The process includes reacting a reaction mixture comprising magnesium ethoxide (Mg(OEt)2), triethylaluminum (TEAl), and 2-ethylhexanol (2-EHOH) to form magnesium 2-ethyl hexyl alkoxide (Mg(2-EHO)2) and contacting Mg(2-EHO)2 in hexane with a first agent to form a reaction product “A.” The process further includes contacting the reaction product “A” with a second agent to form a reaction product “B”, wherein the second agent includes a transition metal and a halogen. The process further includes contacting the reaction product “B” with a third agent to form a reaction product “C”, wherein the third agent includes a first metal halide. In addition, the process includes contacting the reaction product “C” with a fourth agent to form a reaction product “D”, wherein the fourth agent includes a second metal halide. The process also includes contacting the reaction product “D” with a fifth agent to form a Ziegler-Natta catalyst, wherein the fifth agent includes an organoaluminum compound.

    Formation of a Ziegler-Natta catalyst

    公开(公告)号:US09624321B2

    公开(公告)日:2017-04-18

    申请号:US14304358

    申请日:2014-06-13

    Abstract: A process of forming a Ziegler-Natta catalyst component is disclosed. The process includes contacting an alkyl magnesium compound with an alcohol and a first organoaluminum compound to form a magnesium dialkoxide compound and contacting the magnesium dialkoxide compound with a titanating agent to form reaction product “A.” The process further includes reacting reaction product “A” with a halogenating agent to form reaction product “B” and reacting reaction product “B” with a second organoaluminum compound to form a single halogenated catalyst component.

    PELLETS OF LIGHTLY VIS-BROKEN POLYPROPYLENE
    288.
    发明申请
    PELLETS OF LIGHTLY VIS-BROKEN POLYPROPYLENE 审中-公开
    轻质VIS-BROKEN聚丙烯薄膜

    公开(公告)号:US20170051118A1

    公开(公告)日:2017-02-23

    申请号:US14832350

    申请日:2015-08-21

    Abstract: A process including vis-breaking of polypropylene in the presence of 3,6,9-triethyl-3,6,9-trimethyl-1,4,7-triperoxonane to obtain vis-broken polypropylene is provided. The vis-broken polypropylene may be pelletized to obtain pellets. A ratio of a melt flow rate (MI2) of the pellets to a melt flow rate (MI2) of the polypropylene prior to the vis-breaking may be greater than 1:1 and at most 4:1. The pellets may be used to form articles.

    Abstract translation: 提供了一种包括在3,6,9-三乙基-3,6,9-三甲基-1,4,7-三过氧苯甲酸存在下的聚丙烯的断裂以获得可折断的聚丙烯的方法。 可以将可见光聚丙烯造粒以获得颗粒。 颗粒之间的熔体流动速率(MI2)与破坏前的聚丙烯的熔体流动速率(MI2)之比可以大于1:1,最多为4:1。 颗粒可用于形成制品。

    Process for the reduction of alkylation catalyst deactivation utilizing low silica to alumina ratio catalyst
    290.
    发明授权
    Process for the reduction of alkylation catalyst deactivation utilizing low silica to alumina ratio catalyst 有权
    使用低二氧化硅与氧化铝比的催化剂还原烷基化催化剂失活的方法

    公开(公告)号:US09556084B2

    公开(公告)日:2017-01-31

    申请号:US14154422

    申请日:2014-01-14

    Abstract: Alkylation systems and methods of minimizing alkylation catalyst regeneration are described herein. The alkylation systems generally include a preliminary alkylation system adapted to receive an input stream including an alkyl aromatic hydrocarbon and contact the input stream with a preliminary alkylation catalyst disposed therein to form a first output stream. The preliminary alkylation catalyst generally includes a zeolite catalyst having a SiO2/Al2O3 ratio of less than about 25. The alkylation systems further include a first alkylation system adapted to receive the first output stream and contact the first output stream with a first alkylation catalyst disposed therein and an alkylating agent to form a second output stream.

    Abstract translation: 本文描述了使烷基化催化剂再生最小化的烷基化系统和方法。 烷基化系统通常包括适于接收包含烷基芳族烃的输入流并将输入流与设置在其中的预置烷基化催化剂接触以形成第一输出流的初步烷基化系统。 初步烷基化催化剂通常包括SiO 2 / Al 2 O 3比小于约25的沸石催化剂。烷基化系统还包括适于接收第一输出流并将第一输出流与置于其中的第一烷基化催化剂接触的第一烷基化系统 和烷基化剂以形成第二输出流。

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