Supported Catalyst for Olefin Polymerization, Preparation Method and Use Thereof
    231.
    发明申请
    Supported Catalyst for Olefin Polymerization, Preparation Method and Use Thereof 审中-公开
    用于烯烃聚合的负载催化剂,其制备方法和用途

    公开(公告)号:US20160152738A1

    公开(公告)日:2016-06-02

    申请号:US14904691

    申请日:2014-06-20

    Abstract: A supported catalyst for olefin polymerization, a preparation method and use thereof. The catalyst comprises a porous carrier A, a magnesium-containing carrier B, and a supported active component containing a transitional metal of titanium. The catalyst is a highly efficient Ziegler-Natta titanium-based catalyst having a composite support formed by a magnesium compound and a silicon compound, wherein the raw material for the magnesium compound may be any soluble magnesium salt. The supported catalyst may be used for preparing olefin homopolymers or olefin copolymers. According to the present invention, the molecular weight, molecular weight distribution of the olefin homopolymer or olefin copolymer as well as the contents and distribution of the comonomers may be adjusted conveniently by means of changing the factors such as types and amounts of organometallic co-catalyst and molecular weight regulator.

    Abstract translation: 用于烯烃聚合的负载催化剂,其制备方法和用途。 催化剂包括多孔载体A,含镁载体B和含钛过渡金属的负载活性组分。 催化剂是具有由镁化合物和硅化合物形成的复合载体的高效齐格勒 - 纳塔钛基催化剂,其中镁化合物的原料可以是任何可溶的镁盐。 负载催化剂可用于制备烯烃均聚物或烯烃共聚物。 根据本发明,可以通过改变诸如有机金属助催化剂的类型和量的因素来方便地调节烯烃均聚物或烯烃共聚物的分子量,分子量分布以及共聚单体的含量和分布 和分子量调节剂。

    METHOD AND APPARATUS FOR IMPROVING HYDROGEN UTILIZATION RATE OF HYDROGENATION APPARATUS
    233.
    发明申请
    METHOD AND APPARATUS FOR IMPROVING HYDROGEN UTILIZATION RATE OF HYDROGENATION APPARATUS 审中-公开
    提高氢化装置氢化利用率的方法和装置

    公开(公告)号:US20160038854A1

    公开(公告)日:2016-02-11

    申请号:US14764178

    申请日:2014-01-10

    Abstract: A method and apparatus for improving a hydrogen utilization rate in a hydrogenation hot high-pressure separation process. Hydrogenated distillate oil, a gas product and hydrogen pass through an inertia separation distributor arranged in an inlet of a hot high-pressure separator under high pressure for preliminary gas-liquid separation, and a gas phase goes to a subsequent system; a liquid phase goes into a hot low-pressure separator. Releases a part of low-pressure separated gas (mainly hydrogen) after preliminary separation through an injection flash separator in the hot low-pressure separator, and is divided into a gas phase and a liquid phase based on gravitational settling; hydrogen and some micro bubbles that are still dissolved in hot low-pressure separated oil under the pressure are separated from the oil through a centrifugal degassing device; the gas phase exits from the apparatus after carried liquid droplets are removed completely through hydrocyclone separation or coalescence separation, and distillate oil goes to a subsequent facility.

    Abstract translation: 一种用于提高氢化热高压分离工艺中氢利用率的方法和装置。 氢化馏出油,气体产物和氢气通过布置在高压分离器的高压分离器的入口处的预定气液分离的惯性分离分配器,气相进入后续系统; 液相进入热的低压分离器。 通过热式低压分离器中的注射闪蒸分离器预先分离出一部分低压分离气体(主要是氢气),并基于重力沉降分为气相和液相; 在压力下仍然溶解在热的低压分离油中的氢气和一些微气泡通过离心脱气装置与油分离; 在通过水力旋流器分离或聚结分离完全移除载运液滴后,气相从设备中排出,馏出油进入后续设施。

Patent Agency Ranking