公开(公告)号：US09567535B2

公开(公告)日：2017-02-14

申请号：US14191621

申请日：2014-02-27

Applicant: UOP LLC

Inventor： Robert S. Haizmann

IPC: C10G47/26 ,  B01J8/08 ,  C10G49/22 ,  B01J8/24

CPC classification number: C10G47/26 ,  B01J8/08 ,  B01J8/24 ,  C10G49/22 ,  C10G2300/1033 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2300/4081 ,  C10G2400/02

Abstract: One exemplary embodiment can include a slurry hydrocracking process. The process can include combining one or more hydrocarbons and a slurry hydrocracking catalyst as a feed to a slurry hydrocracking reaction zone, fractionating an effluent from the slurry hydrocracking reaction zone, separating the pitch from at least a portion of the slurry hydrocracking catalyst, and recycling the suspension to the slurry hydrocracking reaction zone. The slurry hydrocracking catalyst may include a support. Fractionating the effluent may provide a light vacuum gas oil, a heavy vacuum gas oil, and a mixture comprising a pitch and the slurry hydrocracking catalyst. Generally, the separated slurry hydrocracking catalyst is comprised in a suspension.

Abstract translation: 一个示例性实施方案可以包括浆料加氢裂化方法。 该方法可以包括将一种或多种烃和浆料加氢裂化催化剂作为浆料加氢裂化反应区的进料组合，从淤浆加氢裂化反应区分馏出流出物，从沥青加氢裂化催化剂的至少一部分分离沥青，再循环 悬浮液到浆料加氢裂化反应区。 浆料加氢裂化催化剂可以包括载体。 对流出物进行分馏可以提供轻质真空瓦斯油，重质减压瓦斯油，以及包含沥青和浆料加氢裂化催化剂的混合物。 通常，分离的浆料加氢裂化催化剂包含在悬浮液中。

公开(公告)号：US20170029711A1

公开(公告)日：2017-02-02

申请号：US15189428

申请日：2016-06-22

Applicant: SarTec Corporation

Inventor： Clayton V. McNeff ,  Larry C. McNeff ,  Daniel Thomas Nowlan ,  Bingwen Yan ,  Peter G. Greuel

IPC: C10G3/00 ,  B01J8/08 ,  B01J35/00 ,  C10L1/04 ,  B01J21/06

CPC classification number: C10G3/44 ,  B01J3/008 ,  B01J8/087 ,  B01J8/10 ,  B01J19/20 ,  B01J21/06 ,  B01J21/066 ,  B01J21/20 ,  B01J35/0013 ,  B01J38/02 ,  B01J2208/00017 ,  B01J2208/00168 ,  B01J2208/00539 ,  B01J2208/00628 ,  B01J2208/00814 ,  B01J2219/00087 ,  B01J2219/00162 ,  B01J2219/00186 ,  C10G3/45 ,  C10G2300/805 ,  C10L1/02 ,  C10L1/023 ,  C10L1/04 ,  C10L3/08 ,  C10L3/106 ,  C10L2200/0469 ,  C10L2270/023 ,  C10L2290/06 ,  C10L2290/50 ,  C11C3/00 ,  Y02P20/544 ,  Y02P30/20

Abstract: Embodiments of the invention include apparatus and systems for hydrocarbon synthesis and methods regarding the same. In an embodiment, the invention includes a method for creating a hydrocarbon product stream comprising reacting a reaction mixture in the presence of a catalyst inside of a reaction vessel to form a product mixture, the reaction mixture comprising a carbon source and water. The temperature inside the reaction vessel can be between 450 degrees Celsius and 600 degrees Celsius and the pressure inside the reaction vessel can be above supercritical pressure for water. In an embodiment, the invention includes an extrusion reactor system for creating a hydrocarbon product stream. The temperature inside the extrusion reactor housing between 450 degrees Celsius and 600 degrees Celsius. Pressure inside the reaction vessel can be above supercritical pressure for water. Other embodiments are also included herein.

Abstract translation: 本发明的实施方案包括用于烃合成的装置和系统及其方法。 在一个实施方案中，本发明包括用于产生烃产物流的方法，包括在反应容器内部的催化剂存在下使反应混合物反应以形成产物混合物，所述反应混合物包含碳源和水。 反应容器内的温度可以在450摄氏度至600摄氏度之间，反应容器内的压力可能超过水的超临界压力。 在一个实施方案中，本发明包括用于产生烃产物流的挤出反应器系统。 挤压反应器内部的温度在450摄氏度到600摄氏度之间。 反应容器内的压力可超过水的超临界压力。 本文还包括其它实施例。

公开(公告)号：US20170002113A1

公开(公告)日：2017-01-05

申请号：US15100498

申请日：2014-11-24

Applicant: SAUDI BASIC INDUSTRIES CORPORATION ,  SABIC GLOBAL TECHNOLOGIES B.V.

Inventor： Yahya Banat ,  Jose Fernando Cevallos-Candau

IPC: C08F10/00 ,  B01J19/06 ,  B01J19/24 ,  B01J8/00 ,  B01J8/08

CPC classification number: C08F10/00 ,  B01J8/0015 ,  B01J8/005 ,  B01J8/085 ,  B01J8/087 ,  B01J19/06 ,  B01J19/246 ,  B01J2208/00752 ,  B01J2208/00761 ,  B01J2208/00938 ,  B01J2219/182 ,  C08F2/34 ,  C08F10/02 ,  C08F10/06 ,  C08F2/01 ,  C08F2/00

Abstract: The invention relates to a system for the continuous polymerization of α-olefin monomers comprising a reactor, a compressor, a cooling unit and an external pipe, wherein the reactor comprises a first outlet for a top recycle stream, wherein the system comprises apparatus, wherein the reactor comprises a first inlet for receiving a bottom recycle stream, wherein the reactor comprises an integral separator, wherein the first inlet of the integral separator is connected to a first outlet, wherein the first outlet for the liquid phase is connected to the second outlet of the reactor for the liquid phase, wherein the external pipe comprises a second inlet for receiving a solid polymerization catalyst, wherein the first outlet of the external pipe is connected to a second inlet of the reactor, wherein the reactor comprises a third outlet, wherein the system comprises a first inlet for receiving a feed.

Abstract translation: 本发明涉及一种用于连续聚合α-烯烃单体的系统，包括反应器，压缩机，冷却单元和外部管，其中反应器包括用于顶部再循环流的第一出口，其中该系统包括装置，其中 反应器包括用于接收底部再循环流的第一入口，其中反应器包括整体分离器，其中整体分离器的第一入口连接到第一出口，其中用于液相的第一出口连接到第二出口 用于液相的反应器，其中所述外管包括用于接收固体聚合催化剂的第二入口，其中所述外管的所述第一出口连接到所述反应器的第二入口，其中所述反应器包括第三出口，其中 该系统包括用于接收进料的第一入口。

公开(公告)号：US09446368B2

公开(公告)日：2016-09-20

申请号：US14481112

申请日：2014-09-09

Applicant: JX NIPPON OIL & ENERGY CORPORATION

Inventor： Koji Shimada ,  Naoya Saito

IPC: B01J8/24 ,  B01J8/18 ,  C10G11/18 ,  B01F5/04 ,  B01J8/08 ,  B01J8/00 ,  B01J8/12

CPC classification number: B01J8/245 ,  B01F5/048 ,  B01J8/003 ,  B01J8/004 ,  B01J8/085 ,  B01J8/12 ,  B01J8/1881 ,  B01J2208/00752 ,  B01J2208/00769 ,  B01J2208/00902 ,  B01J2208/00938 ,  C10G11/18

Abstract: A mixing device used in a fluidized catalytic cracking apparatus which mixes feed and a catalyst includes a cylindrical reaction container which supplies a catalyst in a vertical direction; a plurality of feed injection nozzles arranged along an outer circumference of the reaction container; and a catalyst flow regulator which is provided in the reaction container and regulates a flow of the catalyst in the vicinity of the feed injection nozzles. The catalyst flow regulator has no feed supply function and forms a catalyst moving bed having a hollow tubular shape which is coaxial with the reaction container in the vicinity of the feed injection nozzles. The catalyst flow regulator can effectively prevent backward flow of injected fuel. Although the mixing device has a simple structure, it has a high cracking rate and maintenance of the fluidized catalytic cracking apparatus can be performed easier.

Abstract translation: 用于混合进料和催化剂的流化催化裂化装置中的混合装置包括在垂直方向供应催化剂的圆柱形反应容器; 沿着反应容器的外周布置的多个进料喷嘴; 以及催化剂流量调节器，其设置在反应容器中并调节催化剂在进料喷嘴附近的流动。 催化剂流量调节器没有进料供给功能，并且形成具有中空管状形状的催化剂移动床，其在进料喷嘴附近与反应容器同轴。 催化剂流量调节器可以有效地防止喷射燃料的反向流动。 尽管混合装置具有简单的结构，但是其开裂速度高，流化催化裂化装置的维护更容易。

公开(公告)号：US09381487B2

公开(公告)日：2016-07-05

申请号：US14347255

申请日：2012-09-10

Applicant: Frederic Bazer-Bachi ,  Frederic Augier ,  Yacine Haroun ,  Christophe Boyer

Inventor： Frederic Bazer-Bachi ,  Frederic Augier ,  Yacine Haroun ,  Christophe Boyer

IPC: B01J8/08 ,  B01J8/12 ,  B01J19/00 ,  B01J8/04 ,  B01J8/00 ,  B01J8/02 ,  C10G49/00

CPC classification number: B01J19/0053 ,  B01J8/008 ,  B01J8/0278 ,  B01J8/0492 ,  B01J2219/00761 ,  C10G49/002 ,  C10G2300/202

Abstract: The present invention concerns a plate for distributing a polyphase mixture in a reactor operating in trickle bed mode constituted by at least one gas phase and at least one liquid phase, the plate (10) being located above a bed of catalytic particles, comprising a plurality of chimneys (3), characterized in that a portion of the chimneys of the plate located near to the wall of the chamber of the reactor, those termed the peripheral chimneys, have an upper portion which is inclined at an angle with respect to the vertical.The invention also concerns the use of the plate in a reactor with a view to carrying out hydrotreatment, hydrogenation or oxidation reactions.

Abstract translation: 本发明涉及一种用于在由至少一个气相和至少一个液相构成的滴流床模式下操作的反应器中分配多相混合物的板，所述板（10）位于催化颗粒床之上，包括多个 的烟囱（3）的特征在于，位于所述反应器的室的壁附近的那些位于所述反应器的室的那些烟囱的那些部分被称为周边烟囱，具有相对于垂直方向倾斜一定角度的上部 。 本发明还涉及在反应器中使用板，以便进行加氢处理，氢化或氧化反应。

公开(公告)号：US20160176779A1

公开(公告)日：2016-06-23

申请号：US14976559

申请日：2015-12-21

Applicant: Pioneer Energy Inc.

Inventor： Robert M. Zubrin ,  Stacy L. Carrera ,  Mark Berggren

IPC: C07C2/76 ,  B01J8/08 ,  B01J8/02 ,  B01J8/04 ,  C07C2/42 ,  C07C5/333

CPC classification number: C07C2/76 ,  B01J8/0285 ,  B01J8/04 ,  B01J29/48 ,  B01J29/90 ,  B01J38/14 ,  B01J2229/186 ,  C07C5/3332 ,  C07C2529/48 ,  C10G50/00 ,  C10G2300/1081 ,  C10G2400/30 ,  Y02P20/52 ,  Y02P20/584 ,  C07C11/04 ,  C07C15/04 ,  C07C15/06 ,  C07C15/08 ,  C07C15/24

Abstract: This invention pertains to the thermal catalytic synthesis of aromatic compounds from ethane and ethylene. Such synthesis converts lower-value compounds that can only be stored as a gas or liquid under high pressure to a more-valuable liquid compound that can be stored at ambient pressure. The resulting aromatic product is useful as a chemical feedstock or as fuel.

Abstract translation: 本发明涉及从乙烷和乙烯进行芳族化合物的热催化合成。 这种合成将低价值化合物转化成只能在高压下作为气体或液体储存成可在环境压力下储存的更有价值的液体化合物。 得到的芳香族产物可用作化学原料或燃料。

公开(公告)号：US09340469B2

公开(公告)日：2016-05-17

申请号：US14260612

申请日：2014-04-24

Applicant: SHELL OIL COMPANY

Inventor： Leslie Andrew Chewter ,  Hubertus Wilhelmus Albertus Dries ,  Rene Samson ,  Mao Ye

IPC: C07C1/20 ,  C07C1/22 ,  B01J8/00 ,  B01J8/18 ,  B01J8/26 ,  B01J8/28 ,  B01J8/38 ,  B01J29/90 ,  C10G11/18 ,  C10G3/00 ,  B01J8/08 ,  C10G11/16

CPC classification number: C07C1/22 ,  B01J8/0015 ,  B01J8/0055 ,  B01J8/08 ,  B01J8/18 ,  B01J8/1809 ,  B01J8/1863 ,  B01J8/1872 ,  B01J8/26 ,  B01J8/28 ,  B01J8/388 ,  B01J29/90 ,  B01J2208/00548 ,  B01J2208/00557 ,  B01J2208/00761 ,  B01J2208/00769 ,  C07C1/20 ,  C10G3/49 ,  C10G3/57 ,  C10G11/16 ,  C10G11/18 ,  C10G11/182 ,  C10G2300/1081 ,  C10G2300/1088 ,  C10G2300/802 ,  C10G2400/02 ,  C10G2400/20 ,  C10G2400/22 ,  Y02P20/584 ,  Y02P30/20 ,  C07C11/02

Abstract: A catalyst return apparatus is disclosed as well as a riser reactor system comprising the conduit apparatus and a riser reactor, the conduit apparatus comprising a catalyst return conduit and at least two flow control devices in series, each flow control device arranged to control the flow of fluid through the conduit, wherein the length of the catalyst return conduit is more than 20 m. A process for reacting a feedstock in a riser reactor system comprising a riser reactor, the catalyst return apparatus and, and a stage vessel, the process comprising: holding a fluid comprising the catalyst in the at least one stage vessel for a residence time of at least 10 seconds.

Abstract translation: 公开了一种催化剂返回装置以及包括导管装置和提升管反应器的提升管反应器系统，该导管装置包括催化剂返回导管和串联的至少两个流量控制装置，每个流量控制装置被布置成控制流动 流体通过导管，其中催化剂返回导管的长度大于20μm。 一种用于在提升管反应器系统中使原料反应的方法，其包括提升管反应器，催化剂返回装置和阶段容器，该方法包括：将包含催化剂的流体保持在至少一个级容器中用于停留时间 至少10秒钟。

公开(公告)号：US09339780B2

公开(公告)日：2016-05-17

申请号：US14099451

申请日：2013-12-06

Applicant: IFP Energies Nouvelles

Inventor： Eric Sanchez ,  Gilles Ferschneider ,  Frederic Bazer-Bachi

IPC: C10G35/04 ,  C07C6/04 ,  B01J8/00 ,  B01J8/08 ,  B01J8/12 ,  C07C5/27 ,  C07C6/06 ,  C10G35/12

CPC classification number: B01J8/0015 ,  B01J8/003 ,  B01J8/0085 ,  B01J8/085 ,  B01J8/12 ,  C07C5/2702 ,  C07C5/277 ,  C07C6/04 ,  C07C6/06 ,  C07C9/06 ,  C07C11/06 ,  C10G35/12 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2400/02 ,  C10G2400/20 ,  C10G2400/22 ,  C07C9/14

Abstract: The invention describes a radial bed catalytic conversion unit having an outer cylindrical chamber (1), an inner chamber (2) which is also cylindrical, the annular zone included between the outer chamber and the inner chamber, termed the reaction zone (I), being filled with catalyst under slow gravitational flow, and the feed being introduced via an inlet pipe (E), connected to an intermediate box (F) which is in turn connected to a plurality of distribution tubes (3) disposed inside the reaction zone (I) in the vicinity of the outer chamber (1).

Abstract translation: 本发明描述了一种径向床催化转化装置，其具有外圆筒室（1），也是圆柱形的内室（2），包括在外室和内室之间的环形区域，称为反应区（I） 在慢重力流下填充有催化剂，并且进料通过入口管（E）引入，入口管（E）连接到中间箱（F），中间箱（F）又连接到设置在反应区内的多个分配管（3） I）在外室（1）附近。

公开(公告)号：US20160068766A1

公开(公告)日：2016-03-10

申请号：US14848657

申请日：2015-09-09

Applicant: IFP Energies nouvelles

Inventor： Frederic BAZER-BACHI ,  Eric LEMAIRE ,  Fabian LAMBERT

IPC: C10G59/02 ,  B01J8/00 ,  B01J8/08 ,  B01J38/44 ,  B01J38/16

CPC classification number: C10G59/02 ,  B01J8/0015 ,  B01J8/085 ,  B01J8/125 ,  B01J38/16 ,  B01J38/22 ,  B01J38/44 ,  B01J2208/00752 ,  C10G35/10 ,  C10G2300/70

Abstract: The present invention concerns a moving bed catalyst regenerator (1) comprising a vessel (2) extending in a vertical direction, said vessel being divided into at least two regeneration zones extending along the vertical height of said vessel, in which particles of catalyst move under gravity, in which each regeneration zone comprises, in succession and in the order in which the catalysts move: a) a combustion section (CO); b) an oxychlorination section (O) disposed below the combustion section and comprising means for bringing catalyst from the combustion section (CO) to the oxychlorination section (O); c) a calcining section (CA) disposed below the oxychlorination section; characterized in that the regeneration zones are separated from each other by a separation means which is impermeable to catalysts and to gases in a manner such that the catalysts of each of the zones are capable of being regenerated under different operating conditions.

Abstract translation: 本发明涉及一种移动床催化剂再生器（1），其包括在垂直方向上延伸的容器（2），所述容器被分成至少两个沿着所述容器的垂直高度延伸的再生区，其中催化剂颗粒在下方移动 重力，其中每个再生区依次包括和催化剂移动的顺序：a）燃烧段（CO）; b）设置在燃烧部分下方的氧氯化部分（O），并且包括用于将来自燃烧部分（CO）的催化剂引入氧氯化部分（O）的装置; c）设置在氧氯化部分下方的煅烧部分（CA）; 其特征在于，所述再生区域通过分离装置相互分离，所述分离装置对催化剂和气体是不可渗透的，使得每个区域的催化剂能够在不同的操作条件下再生。

公开(公告)号：US09243752B2

公开(公告)日：2016-01-26

申请号：US14365628

申请日：2012-09-06

Applicant: Hee Jin Kang ,  Dong Kon Lee ,  Jin Choi

Inventor： Hee Jin Kang ,  Dong Kon Lee ,  Jin Choi

IPC: C01B6/00 ,  B01J8/08 ,  C07C9/00 ,  F17C5/00 ,  C10L3/06 ,  F17C1/12 ,  F17C3/00 ,  C10L3/10

CPC classification number: F17C5/00 ,  C10L3/06 ,  C10L3/107 ,  C10L3/108 ,  F17C1/12 ,  F17C3/00 ,  F17C2201/0109 ,  F17C2201/035 ,  F17C2201/052 ,  F17C2201/054 ,  F17C2203/03 ,  F17C2205/0107 ,  F17C2205/0126 ,  F17C2205/0192 ,  F17C2205/0323 ,  F17C2205/0394 ,  F17C2221/03 ,  F17C2221/036 ,  F17C2223/0176 ,  F17C2225/0123 ,  F17C2227/0304 ,  F17C2227/0316 ,  F17C2227/0337 ,  F17C2227/0379 ,  F17C2227/0381 ,  F17C2250/043 ,  F17C2250/0439 ,  F17C2265/03 ,  F17C2265/031 ,  F17C2265/05

Abstract: Disclosed is a container for storing, transporting, and dissociating hydrate pellets, the container comprising: a first container (100) made up of a plurality of frames; a second container (200) which is rotatably installed inside the first container (100), stores hydrate pellets therein, and has an internal surface to which a heat insulating member is attached; and a refrigerating machine (300) which is installed inside the first container (100) and refrigerates the second container (200), wherein the second container (200) is equipped with a heating wire (210), which is heated to dissociate the hydrate pellets by being supplied with power, or with a hot water tube (220), through which hot water flows to dissociate the hydrate pellets, on the internal surface thereof.

Abstract translation: 公开了一种用于储存，运输和解离水合物丸粒的容器，该容器包括：由多个框架构成的第一容器（100） 可旋转地安装在第一容器（100）内的第二容器（200）在其中存储水合物丸粒，并且具有安装绝热构件的内表面; 以及安装在第一容器（100）的内部并使第二容器（200）冷藏的冷冻机（300），其中，第二容器（200）配备有加热线（210），加热线将水合物 通过供给动力的颗粒，或者在热水管（220）上流动热水以在其内表面解离水合物丸粒。