Procatalyst particles and polymerization process for impact copolymers

    公开(公告)号:US10059784B2

    公开(公告)日:2018-08-28

    申请号:US15036365

    申请日:2014-11-26

    Abstract: Particles of a procatalyst composition having a particle size D50 from 19 microns to 30 microns. A polymerization process comprising halogenating, in the presence of a substituted phenylene aromatic diester, particles of a MagTi procatalyst precursor to form particles of a procatalyst composition having a particle size D50 from 19 microns to 30 microns; first contacting a propylene and optionally one or more first comonomers with a catalyst composition comprising the particles of the procatalyst composition in a first polymerization reactor to form an active propylene-based polymer; and second contacting the active propylene-based polymer with at least one second comonomer in a second polymerization reactor to form a propylene impact copolymer.

    Gas-phase polymerization process with wet zone
    2.
    发明授权
    Gas-phase polymerization process with wet zone 有权
    湿区气相聚合工艺

    公开(公告)号:US09556291B2

    公开(公告)日:2017-01-31

    申请号:US15021561

    申请日:2014-09-11

    CPC classification number: C08F110/06 C08F2/34 C08F10/06 C08F210/06 C08F210/16

    Abstract: The present disclosure is directed to a process for producing olefin-based polymer in a gas phase polymerization reactor. The process includes forming a wet zone in the gas phase polymerization reactor. The wet zone is formed by maintaining a temperature less than or equal to the fluidizing medium dew point temperature+2° C. in a region of the reactor. The region is defined as the region extending from the distributor plate to 2.5 meters above the distributor plate. Injection of a high activity catalyst composition in the wet zone produces olefin-based having a settled bulk density greater than 23.5 lb/ft3.

    Abstract translation: 本公开涉及在气相聚合反应器中制备烯烃基聚合物的方法。 该方法包括在气相聚合反应器中形成湿区。 通过在反应器的区域中保持小于或等于流化介质露点温度+ 2℃的温度来形成湿区。 该区域被定义为从分配器板延伸到分配板上方2.5米的区域。 在湿区中注入高活性催化剂组合物产生具有大于23.5lb / ft 3的沉降堆积密度的烯烃基。

    PROCATALYST PARTICLES AND POLYMERIZATION PROCESS FOR IMPACT COPOLYMERS
    3.
    发明申请
    PROCATALYST PARTICLES AND POLYMERIZATION PROCESS FOR IMPACT COPOLYMERS 审中-公开
    用于冲击共聚物的方法颗粒和聚合方法

    公开(公告)号:US20160297906A1

    公开(公告)日:2016-10-13

    申请号:US15036365

    申请日:2014-11-26

    CPC classification number: C08F210/06 C08F2/001 C08F4/651

    Abstract: Particles of a procatalyst composition having a particle size D50 from 19 microns to 30 microns. A polymerization process comprising halogenating, in the presence of a substituted phenylene aromatic diester, particles of a MagTi procatalyst precursor to form particles of a procatalyst composition having a particle size D50 from 19 microns to 30 microns; first contacting a propylene and optionally one or more first comonomers with a catalyst composition comprising the particles of the procatalyst composition in a first polymerization reactor to form an active propylene-based polymer; and second contacting the active propylene-based polymer with at least one second comonomer in a second polymerization reactor to form a propylene impact copolymer.

    Abstract translation: 具有19微米至30微米的粒度D50的主催化剂组合物的颗粒。 聚合方法包括在取代的亚苯基芳族二酯的存在下,将MagTi原催化剂前体的颗粒卤化以形成粒径D 50为19微米至30微米的前催化剂组合物的颗粒; 首先在第一聚合反应器中使丙烯和任选的一种或多种第一共聚单体与包含前催化剂组合物的颗粒的催化剂组合物接触以形成活性丙烯基聚合物; 以及在第二聚合反应器中使活性丙烯类聚合物与至少一种第二共聚单体接触,以形成丙烯抗冲共聚物。

    PROPYLENE-BASED POLYMER WITH REDUCED HIGH-MOLECULAR WEIGHT PORTION
    4.
    发明申请
    PROPYLENE-BASED POLYMER WITH REDUCED HIGH-MOLECULAR WEIGHT PORTION 有权
    具有降低高分子重量份的丙烯聚合物

    公开(公告)号:US20160280812A1

    公开(公告)日:2016-09-29

    申请号:US15035649

    申请日:2014-11-14

    Abstract: The present disclosure provides a process for producing propylene-based polymer. The process includes contacting, under polymerization conditions in a gas phase polymerization reactor, propylene monomer and optionally one or more comonomers with a Ziegler-Natta catalyst composition. The process includes maintaining the temperature of a reaction zone of the reactor at a temperature from greater than 72° C. to less than or equal to 85° C., and forming a propylene-based polymer having a molecular weight (Mw) greater than 100,000, and a Mz+1/Mz less than 2.20. The resultant propylene-based polymer is advantageous in fiber applications.

    Abstract translation: 本公开内容提供了一种生产基于丙烯的聚合物的方法。 该方法包括在气相聚合反应器中的聚合条件下使丙烯单体和任选的一种或多种共聚单体与齐格勒 - 纳塔催化剂组合物接触。 该方法包括将反应器的反应区的温度保持在大于72℃至小于或等于85℃的温度,并形成分子量(Mw)大于 100,000,Mz + 1 / Mz小于2.20。 得到的丙烯类聚合物在纤维应用中是有利的。

    Process for efficient polymer particle purging

    公开(公告)号:US11578146B2

    公开(公告)日:2023-02-14

    申请号:US17381355

    申请日:2021-07-21

    Abstract: A process comprising polymerizing olefin monomers and optionally comonomers in a first reactor vessel, thereby forming a raw product stream comprising polymerized solids, unreacted monomer and optionally comonomer, the polymerized solids comprising olefin polymer, volatile organic compounds (VOC) and catalyst system. Then the polymerized solids are contacted with a catalyst poison selected from carbon monoxide, carbon dioxide, oxygen, water, alcohols, amines, or mixtures thereof, thereby forming a passivated stream. The passivated stream is maintained in an agitated state within a second reactor. The passivated stream within the second reactor is then contacted with a circulating gas comprising unreacted monomer for a residence time, thereby reducing the concentration of VOC in the polymerized solids by at least 10 wt % compared to the level before entering the second reactor, thereby forming a purified olefin polymer solids stream.

    PRODUCING HIGH COMONOMER CONTENT PROPYLENE-BASED POLYMERS.
    8.
    发明申请
    PRODUCING HIGH COMONOMER CONTENT PROPYLENE-BASED POLYMERS. 审中-公开
    生产高性能内容丙烯聚合物。

    公开(公告)号:US20160289357A1

    公开(公告)日:2016-10-06

    申请号:US15035985

    申请日:2014-11-21

    Abstract: A gas-phase process for making a propylene-based polymer in a fluidized-bed reactor, the reactor containing a fluidized bed including polymer product particles and a catalyst, the process having a set of quantitative criteria for maximum monomer partial pressure, maximum reactor temperature, and comonomer content(s) in the propylene-based polymer. The propylene-based polymer may be EBPT or BPRCP. The catalyst may include a catalyst/donor system comprising (1) a supported Ziegler-Natta pro-catalyst, (2) a co-catalyst, and (3) a mixed external electron donor system including (a) an activity limiting agent including at least one carboxylate ester functional group, and (b) a selectivity control agent.

    Abstract translation: 一种用于在流化床反应器中制备丙烯基聚合物的气相方法,该反应器含有包含聚合物产物颗粒和催化剂的流化床,该方法具有一组用于最大单体分压,最大反应器温度的定量标准 ,和丙烯类聚合物中的共聚单体含量。 基于丙烯的聚合物可以是EBPT或BPRCP。 催化剂可以包括催化剂/给体系统,其包括(1)负载的齐格勒 - 纳塔催化剂,(2)助催化剂,和(3)混合的外部电子给体系统,其包含(a)活性限制剂, 至少一个羧酸酯官能团,和(b)选择性控制剂。

    PROPYLENE ETHYLENE RANDOM COPOLYMER SUITABLE FOR PIPE
    9.
    发明申请
    PROPYLENE ETHYLENE RANDOM COPOLYMER SUITABLE FOR PIPE 审中-公开
    丙烯乙烯随机共聚物适用于管道

    公开(公告)号:US20160251462A1

    公开(公告)日:2016-09-01

    申请号:US15030786

    申请日:2014-10-28

    Abstract: A composition is provided which comprises a propylene ethylene random copolymer having a melt flow rate (MFR) (as determined according to ASTM D1238, 230° C., 2.16 Kg) of less than 1 g/10 min, a xylene solubles content of less than 7% by weight, an ethylene content of from 3 to 5 percent by weight of the copolymer, and a value equal to or greater than 92 for the product of the Koenig B value times the % mm triads measured on the xylene insoluble fraction of the random copolymer obtained by the wet method. Pipes made from the composition demonstrate improved pressure endurance.

    Abstract translation: 提供了一种组合物,其包含丙烯乙烯无规共聚物,其熔体流动速率(MFR)(根据ASTM D1238测定,230℃,2.16Kg)小于1g / 10分钟,二甲苯可溶物含量少 超过7重量%,乙烯含量为共聚物重量的3至5重量%,并且对于Koenig B值乘以在二甲苯不溶部分测量的%mm三单元组的乘积,等于或大于92的值 通过湿法获得的无规共聚物。 由该组合物制成的管道显示出改善的耐压性能。

    GAS-PHASE POLYMERIZATION PROCESS WITH WET ZONE
    10.
    发明申请
    GAS-PHASE POLYMERIZATION PROCESS WITH WET ZONE 有权
    带有湿区的气相聚合工艺

    公开(公告)号:US20160229933A1

    公开(公告)日:2016-08-11

    申请号:US15021561

    申请日:2014-09-11

    CPC classification number: C08F110/06 C08F2/34 C08F10/06 C08F210/06 C08F210/16

    Abstract: The present disclosure is directed to a process for producing olefin-based polymer in a gas phase polymerization reactor. The process includes forming a wet zone in the gas phase polymerization reactor. The wet zone is formed by maintaining a temperature less than or equal to the fluidizing medium dew point temperature+2° C. in a region of the reactor. The region is defined as the region extending from the distributor plate to 2.5 meters above the distributor plate. Injection of a high activity catalyst composition in the wet zone produces olefin-based having a settled bulk density greater than 23.5 lb/ft3.

    Abstract translation: 本公开涉及在气相聚合反应器中制备烯烃基聚合物的方法。 该方法包括在气相聚合反应器中形成湿区。 通过在反应器的区域中保持小于或等于流化介质露点温度+ 2℃的温度来形成湿区。 该区域被定义为从分配器板延伸到分配板上方2.5米的区域。 在湿区中注入高活性催化剂组合物产生具有大于23.5lb / ft 3的沉降堆积密度的烯烃基。

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