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    Process for improving the polymerization of ethylene and one or more optional comonomer(s) in a polymerization loop reactor
    33.
    发明授权
    Process for improving the polymerization of ethylene and one or more optional comonomer(s) in a polymerization loop reactor 有权
    改进聚合反应器中乙烯和一种或多种任选的共聚单体聚合的方法

    公开(公告)号：US09162204B2

    公开(公告)日：2015-10-20

    申请号：US13693501

    申请日：2012-12-04

    Applicant: TOTAL RESEARCH & TECHNOLOGY FELUY

    Inventor： Daan Dewachter

    IPC: F01N3/20 ,  B01J19/00 ,  B01J19/18 ,  C08F2/00 ,  C08F210/00 ,  B01J8/08 ,  B01J8/00 ,  C08F10/02 ,  C08F110/02 ,  C08F210/16

    CPC classification number: B01J8/08 ,  B01J8/007 ,  B01J19/18 ,  B01J2219/00094 ,  B01J2219/00164 ,  C08F10/02 ,  C08F110/02 ,  C08F210/16 ,  C08F2/001 ,  C08F2/14 ,  C08F210/14

    Abstract: The present invention relates to a process for improving the polymerization of ethylene and one or more optional co-monomer(s) in a polymerization loop reactor characterized in that said process comprises the step of controlling the hydrogen/monomer ratio along the path of the reactor by multiple, spatially separated, feeding of hydrogen along the path of the loop reactor. In particular, the invention provides a process for controlling, and preferably narrowing, the molecular weight distribution of the produced polymer particles. In another aspect, the invention relates to a polymerization loop reactor suitable for the polymerization process of ethylene and an optional olefin co-monomer, wherein the molecular weight distribution of the produced ethylene polymer can be controlled.

    Abstract translation: 本发明涉及在聚合反应器反应器中改进乙烯和一种或多种任选的共聚单体聚合的方法，其特征在于所述方法包括沿着反应器的路径控制氢/单体比例的步骤 通过多个空间分离，沿着环管反应器的路径供给氢。 特别地，本发明提供了一种控制所产生的聚合物颗粒的分子量分布并优选变窄的方法。 另一方面，本发明涉及适用于乙烯和任选的烯烃共聚单体的聚合方法的聚合反应器反应器，其中可以控制所生产的乙烯聚合物的分子量分布。

    Combined heavy reformate dealkylation-transalkylation process for maximizing xylenes production
    35.
    发明授权
    Combined heavy reformate dealkylation-transalkylation process for maximizing xylenes production 有权
    用于最大化二甲苯生产的联合重质重整产物脱烷基 - 烷基转移方法

    公开(公告)号：US09000247B2

    公开(公告)日：2015-04-07

    申请号：US13866559

    申请日：2013-04-19

    Applicant: Saudi Arabian Oil Company

    Inventor： Raed Abudawoud

    IPC: C07C6/12 ,  C07C4/14 ,  C07C4/18 ,  C07C6/06

    CPC classification number: C07C4/18 ,  B01J8/08 ,  B01J8/24 ,  B01J2219/24 ,  C07C4/12 ,  C07C6/06 ,  C07C6/123 ,  C07C6/126 ,  C07C2529/40 ,  C07C2529/70 ,  C10G65/043 ,  C10G2400/30 ,  C07C15/06 ,  C07C15/02 ,  C07C15/08

    Abstract: A method of forming mixed xylenes from a heavy reformate using a dealkylation-transalkylation system includes the step of introducing both a heavy reformate containing methyl ethyl benzenes and tri-methyl benzenes and that is sufficiently free of toluene and a hydrogen-containing material into the dealkylation stage such that the heavy reformate and the hydrogen-containing material intermingle and contact the hydrodealkylation catalyst. The dealkylation-transalkylation system includes dealkylation, non-aromatic product gas separations and transalkylation stages. Toluene forms from the reaction of methyl ethyl benzenes and hydrogen in the presence of the hydrodealkylation catalyst. The method also includes the step of introducing a dealkylated heavy reformate into the transalkylation stage such that the dealkylated heavy reformate contacts a transalkylation catalyst, forming a transalkylation stage product mixture includes mixed xylenes.

    Abstract translation: 使用脱烷基 - 烷基转移体系从重质重整产物形成混合二甲苯的方法包括将含有甲基乙基苯和三甲基苯的重质化合物和足够不含甲苯和含氢材料引入脱烷基化的步骤 使得重质重质化合物和含氢材料混合并与加氢脱烷基化催化剂接触。 脱烷基 - 烷基转移体系包括脱烷基化，非芳族产物气体分离和烷基转移反应。 在加氢脱烷基催化剂的存在下，甲苯与氢的反应形成甲苯。 该方法还包括将脱烷基重质重整产物引入烷基转移反应阶段的步骤，使得脱烷基重质重质化物与烷基转移催化剂接触，形成烷基转移反应产物混合物包括混合二甲苯。

    HYDROCARBON PRODUCTION APPARATUS AND HYDROCARBON PRODUCTION PROCESS
    36.
    发明申请
    HYDROCARBON PRODUCTION APPARATUS AND HYDROCARBON PRODUCTION PROCESS 有权
    石油生产设备和油气生产过程

    公开(公告)号：US20150011662A1

    公开(公告)日：2015-01-08

    申请号：US14004954

    申请日：2012-03-13

    Applicant: Shinya Arai

    Inventor： Shinya Arai

    IPC: B01J8/08 ,  C07C1/02

    CPC classification number: B01J8/08 ,  B01J2208/00796 ,  C07C1/02 ,  C10G2/00 ,  C10G2300/1022 ,  C10G2300/304 ,  C10G2300/4031

    Abstract: The hydrocarbon production apparatus is provided with a gas-liquid separator for cooling gaseous state hydrocarbons drawn out from a gas phase portion of a reactor for the Fischer-Tropsch synthesis reaction and liquefying a portion of the hydrocarbons. A light liquid hydrocarbon supply line for supplying light hydrocarbons is disposed between a downstream side line which is downstream from the last stage of a gas-liquid separating unit of the gas-liquid separator, and an upstream side line which is upstream from the last stage of the gas-liquid separating unit of the gas-liquid separator, wherein the downstream side line is a liquid hydrocarbon line on the downstream side through which the light hydrocarbons having cloud points lower than the temperature at an outlet of a cooler in the last stage of the gas-liquid separating unit are flowed.

    Abstract translation: 烃制造装置设置有用于冷却从费 - 托合成反应的反应器的气相部分抽出的气态烃并液化一部分烃的气液分离器。 用于供给轻质烃的轻液态碳氢化合物供给管路配置在气液分离器的气液分离装置的最后级的下游侧的下游侧管线和最后级的上游侧的上游侧管线 气液分离器的气液分离单元，其中下游侧线是下游侧的液体碳氢化合物管线，其中浊点低于最后阶段的冷却器出口处的温度 的气液分离装置。

    PROCESS AND APPARATUS FOR FLUID CATALYTIC CRACKING
    37.
    发明申请
    PROCESS AND APPARATUS FOR FLUID CATALYTIC CRACKING 审中-公开
    流体催化裂化的工艺和装置

    公开(公告)号：US20140364300A1

    公开(公告)日：2014-12-11

    申请号：US14465268

    申请日：2014-08-21

    Applicant: UOP LLC

    Inventor： Paolo Palmas

    IPC: B01J38/06 ,  B01J21/20 ,  B01J29/90 ,  B01J8/08 ,  C10G11/00

    CPC classification number: C10G11/182 ,  B01J8/0055 ,  B01J8/08 ,  B01J8/26 ,  B01J21/20 ,  B01J29/90 ,  B01J38/06 ,  C10G11/00

    Abstract: One exemplary embodiment can be a process for fluid catalytic cracking. The process can include sending a first catalyst from a first riser reactor and a second catalyst from a second riser reactor to a regeneration vessel having a first stage and a second stage. The first catalyst may be sent to the first stage and the second catalyst may be sent to the second stage of the regeneration vessel. Generally, the first stage is positioned above the second stage.

    Abstract translation: 一个示例性实施方案可以是流化催化裂化的方法。 该方法可以包括将第一催化剂从第一提升管反应器和第二催化剂从第二提升管反应器送到具有第一阶段和第二阶段的再生容器。 可将第一催化剂送至第一阶段，第二催化剂可送至再生容器的第二阶段。 通常，第一阶段位于第二阶段之上。

    Process and apparatus for fluid catalytic cracking
    38.
    发明授权
    Process and apparatus for fluid catalytic cracking 有权
    流化床催化裂化的工艺和装置

    公开(公告)号：US08864979B2

    公开(公告)日：2014-10-21

    申请号：US13425657

    申请日：2012-03-21

    Applicant: Paolo Palmas

    Inventor： Paolo Palmas

    IPC: B01J8/18 ,  B01J8/24 ,  B01J8/26 ,  C10G51/06 ,  C10G11/18 ,  C10G11/05

    CPC classification number: C10G11/182 ,  B01J8/0055 ,  B01J8/08 ,  B01J8/26 ,  B01J21/20 ,  B01J29/90 ,  B01J38/06 ,  C10G11/00

    Abstract: One exemplary embodiment can be a process for fluid catalytic cracking. The process can include sending a first catalyst from a first riser reactor and a second catalyst from a second riser reactor to a regeneration vessel having a first stage and a second stage. The first catalyst may be sent to the first stage and the second catalyst may be sent to the second stage of the regeneration vessel. Generally, the first stage is positioned above the second stage.

    Abstract translation: 一个示例性实施方案可以是流化催化裂化的方法。 该方法可以包括将第一催化剂从第一提升管反应器和第二催化剂从第二提升管反应器送到具有第一阶段和第二阶段的再生容器。 可将第一催化剂送至第一阶段，第二催化剂可送至再生容器的第二阶段。 通常，第一阶段位于第二阶段之上。

    SYSTEMS FOR HYDROPROCESSING HEAVY OIL
    40.
    发明申请
    SYSTEMS FOR HYDROPROCESSING HEAVY OIL 有权
    用于加氢重油的系统

    公开(公告)号：US20140093433A1

    公开(公告)日：2014-04-03

    申请号：US14095698

    申请日：2013-12-03

    Applicant: HEADWATERS HEAVY OIL, LLC

    Inventor： Roger K. Lott ,  Lap Keung Lee

    IPC: C10G49/00

    CPC classification number: C10G47/06 ,  B01J8/08 ,  B01J8/22 ,  B01J8/226 ,  C10G45/04 ,  C10G45/16 ,  C10G45/34 ,  C10G45/46 ,  C10G45/56 ,  C10G47/26 ,  C10G49/005 ,  C10G49/12 ,  C10G65/00 ,  C10G65/02 ,  C10G67/08 ,  C10G2300/1033 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2300/202 ,  C10G2300/206 ,  C10G2300/4056 ,  C10G2300/70 ,  C10G2300/703 ,  C10G2300/802

    Abstract: A hydroprocessing system involves introducing heavy oil and in situ formed metal sulfide catalyst particles, or a catalyst precursor capable of forming metal sulfide catalyst particles in situ within the heavy oil, into a hydroprocessing reactor. The metal sulfide catalyst particles are formed in situ by 1) premixing a catalyst precursor with a hydrocarbon diluent to form a precursor mixture, 2) mixing the precursor mixture with heavy oil to form a conditioned feedstock, and 3) heating the conditioned feedstock to decompose the catalyst precursor and cause or allow metal from the precursor to react with sulfur in the heavy oil to form the metal sulfide catalyst particles in situ in the heavy oil. The in situ formed metal sulfide catalyst particles catalyze beneficial upgrading reactions between the heavy oil and hydrogen and eliminates or reduces formation of coke precursors and sediment.

    Abstract translation: 加氢处理系统包括将重油和原位形成的金属硫化物催化剂颗粒或能够在重油内原位形成金属硫化物催化剂颗粒的催化剂前体引入加氢处理反应器。 金属硫化物催化剂颗粒是通过以下步骤形成的：1）将催化剂前体与烃稀释剂预混合以形成前体混合物，2）将前体混合物与重油混合以形成调节原料，和3）加热经调节的原料以分解 催化剂前体并使来自前体的金属与重油中的硫反应，以在重油中原位形成金属硫化物催化剂颗粒。 原位形成的金属硫化物催化剂颗粒催化重油和氢之间的有益升级反应，消除或减少焦炭前体和沉积物的形成。

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