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    FCC UNITS, APPARATUSES AND METHODS
    5.
    发明公开
    FCC UNITS, APPARATUSES AND METHODS 审中-公开
    FCC装置，设备和方法

    公开(公告)号：EP3201294A1

    公开(公告)日：2017-08-09

    申请号：EP15845827.3

    申请日：2015-06-30

    申请人： UOP LLC

    发明人： FREY, Stanley Joseph ,  GU, Weikai

    IPC分类号： C10G11/18 ,  B01J8/24

    CPC分类号： B01J8/1836 ,  B01J8/1827 ,  B01J8/1863 ,  B01J8/1872 ,  B01J8/388 ,  B01J2208/00176 ,  B01J2208/00362 ,  B01J2208/00371 ,  B01J2208/00902 ,  C10G11/187

    摘要： Fluid catalytic cracking (FCC) units, apparatuses, and methods for catalytically cracking a mixture of a pyrolysis oil stream and a hydrocarbon stream are provided herein. In an embodiment, an FCC unit includes a reaction chamber suitable for contacting a pyrolysis oil, a hydrocarbon, and a catalyst. The FCC unit includes a coolant conduit having an coolant outlet in communication with the reaction chamber and suitable for introducing a coolant stream through the coolant outlet into the reaction chamber. The FCC unit further includes a pyrolysis oil conduit including a pyrolysis oil outlet positioned within the coolant conduit and suitable for injecting the pyrolysis oil through the pyrolysis oil outlet into the reaction chamber.

    摘要翻译： 本文提供用于催化裂解热解油物流和烃物流的混合物的流化催化裂化（FCC）单元，设备和方法。 在一个实施方案中，FCC单元包括适用于接触热解油，烃和催化剂的反应室。 FCC单元包括冷却剂导管，该冷却剂导管具有与反应室连通的冷却剂出口，并且适于将冷却剂流通过冷却剂出口引入反应室。 FCC单元还包括热解油导管，其包括位于冷却剂导管内且适合于将热解油通过热解油出口注入到反应室中的热解油出口。

    METHOD AND APPARATUS FOR POLYMERISING OLEFINS IN GAS PHASE
    6.
    发明公开
    METHOD AND APPARATUS FOR POLYMERISING OLEFINS IN GAS PHASE 有权
    VERFAHREN UND VORRICHTUNG ZUR POLYMERISATION VON OLEFINEN IN DER GASPHASE

    公开(公告)号：EP3103818A1

    公开(公告)日：2016-12-14

    申请号：EP15171820.2

    申请日：2015-06-12

    申请人： Borealis AG

    发明人： Kanellopoulos, Vasileios ,  Nyfors, Klaus ,  Aguayo Arellano, Pablo Ivan ,  Weickert, Gunter ,  Prinsen, Eric-Jan

    IPC分类号： C08F2/01 ,  B01J8/08 ,  B01J8/18 ,  B01J8/24 ,  C08F2/34

    CPC分类号： C08F10/02 ,  B01J8/005 ,  B01J8/0055 ,  B01J8/006 ,  B01J8/1818 ,  B01J8/1827 ,  B01J8/1836 ,  B01J8/1863 ,  B01J8/1872 ,  B01J2208/00176 ,  B01J2208/00893 ,  B01J2208/00991 ,  C08F2/01 ,  C08F2/34 ,  C08F2500/07

    摘要： The present invention deals with an olefin polymerisation process. At least one olefin is polymerised in gas phase in a fluidised bed in the presence of an olefin polymerisation catalyst in a polymerisation reactor having a vertical body; a generally conical downwards tapering bottom zone; a generally cylindrical middle zone above and connected to said bottom zone; and a generally conical upwards tapering top zone above and connected to said middle zone. Fluidisation gas is introduced to the bottom zone of the reactor from where it passes upwards through the reactor, and withdrawn from the top zone of the reactor. The gas is then compressed, cooled and returned into the bottom zone of the reactor. A fluidised bed is thus formed within the reactor where the growing polymer particles are suspended in the upwards rising gas stream wherein the superficial velocity of the fluidisation gas is less than the transport velocity of the particles. There is no fluidisation grid in the reactor. The fluidisation gas is passed from an inlet chamber into the bottom zone and the gas flows from the upper part of the inlet chamber to the lower part thereof and the gas flows from the lower part of the inlet chamber to the bottom zone.

    摘要翻译： 本发明涉及烯烃聚合方法。 在具有垂直体的聚合反应器中的烯烃聚合催化剂存在下，在流化床中至少一种烯烃在气相中聚合; 一个大致圆锥形的向下锥形底部区域; 在所述底部区域上方并连接到所述底部区域的大致圆柱形的中间区域; 以及在所述中间区域上方并连接到所述中间区域的大致锥形的向上锥形顶部区域 流化气体被引入到反应器的底部区域，在那里它向上通过反应器，并从反应器的顶部区域排出。 然后将气体压缩，冷却并返回到反应器的底部区域。 因此，在反应器内形成流化床，其中生长的聚合物颗粒悬浮在向上升的气流中，其中流化气体的表观速度小于颗粒的输送速度。 反应器中没有流化栅。 流化气体从入口室进入底部区域，并且气体从入口室的上部流到其下部，并且气体从入口室的下部流动到底部区域。

    Multistage process for the polymerization of olefins
    8.
    发明公开
    Multistage process for the polymerization of olefins 审中-公开
    烯烃聚合的多阶段过程

    公开(公告)号：EP2803680A1

    公开(公告)日：2014-11-19

    申请号：EP13168101.7

    申请日：2013-05-16

    申请人： Basell Polyolefine GmbH

    发明人： Penzo, Giuseppe ,  Mei, Gabriele ,  Meier, Gerhardus ,  Schueller, Ulf ,  Ciarrocchi, Antonio

    IPC分类号： C08F210/00 ,  C08F2/00 ,  C08F2/34

    CPC分类号： C08F110/02 ,  B01J8/0025 ,  B01J8/1863 ,  B01J8/1872 ,  B01J8/26 ,  B01J19/245 ,  B01J2208/00274 ,  B01J2208/00292 ,  B01J2208/00557 ,  B01J2208/00752 ,  B01J2208/00761 ,  B01J2208/00769 ,  B01J2208/00991 ,  B01J2219/24 ,  C08F10/00 ,  C08F2/001 ,  C08F2/34 ,  C08F2/01 ,  C08F2500/12 ,  C08F2500/07 ,  C08F2500/24 ,  C08F2500/18

    摘要： A process for polymerizing olefins at temperatures of from 30°C to 140°C and pressures of from 1.0 MPa to 10 MPa in the presence of a polymerization catalyst in a multistage polymerization of olefins in at least two serially connected gas-phase polymerization reactors, the process for transferring polyolefin particles from a first gas-phase polymerization reactor to a second gas-phase polymerization reactor comprising the steps of
    a) discharging polyolefin particles from the first gas-phase polymerization reactor into a separation chamber in which the polyolefin particles are separated from concomitantly discharged reaction gas, the separation chamber being at a lower pressure than the pressure in the first gas-phase polymerization reactor;
    b) transferring the polyolefin particles within the separation chamber into a lower part of the separation chamber which contains a bed of polyolefin particles which moves from top to bottom of this part of the separation chamber and into which a fluid is introduced in an amount that an upward stream of the fluid in the bed of polyolefin particles above the fluid introduction point is induced,
    c) withdrawing polyolefin particles from the lower end of said lower part and transferring them to one of at least two lock hoppers working intermittently in parallel; and
    d) simultaneously pressurizing another of the at least two lock hoppers working intermittently by means of a gas comprising reaction gas coming from the second gas-phase polymerization reactor, and
    apparatus for the multistage polymerization of olefins, comprising at least two serially connected gas-phase polymerization reactors and a device for transferring polyolefin particles from an upstream gas-phase polymerization reactor to a downstream gas-phase polymerization reactor, the transferring device comprising
    - a gas/solid separation chamber placed downstream of the upstream gas-phase polymerization which gas/solid separation chamber is equipped at a lower part with an inlet for introducing a fluid, and
    - connected to the gas/solid separation chamber at least two lock hoppers, placed in a parallel arrangement, each connected to the downstream gas-phase polymerization reactor.

    摘要翻译： 在至少两个串联连接的气相聚合反应器中，在聚合催化剂存在下，在烯烃的多级聚合反应中，在30℃至140℃的温度和1.0MPa至10MPa的压力下聚合烯烃的方法， 将聚烯烃颗粒从第一气相聚合反应器转移到第二气相聚合反应器的方法包括以下步骤：a）将聚烯烃颗粒从第一气相聚合反应器排出到其中分离聚烯烃颗粒的分离室中 来自伴随排出的反应气体，分离室的压力低于第一气相聚合反应器中的压力; b）将分离室内的聚烯烃颗粒转移到分离室的下部，该分离室包含聚烯烃颗粒床，所述聚烯烃颗粒床从该分离室的该部分的顶部移动到底部并且以这样的量引入流体， 诱导在流体引入点之上的聚烯烃颗粒床中的流体的向上流，c）从所述下部的下端抽出聚烯烃颗粒，并将它们传送到并行间歇工作的至少两个闭锁料斗中的一个; 和d）同时通过包含来自第二气相聚合反应器的反应气体的气体对间歇工作的至少两个闭锁料斗中的另一个进行加压，以及用于烯烃多级聚合的设备，其包括至少两个串联连接的气 - 以及将聚烯烃颗粒从上游气相聚合反应器转移到下游气相聚合反应器的装置，所述转移装置包括：气/固分离室，其置于上游气相聚合的下游，气/ 固体分离室在下部装备有用于引入流体的入口，并且 - 与气体/固体分离室连接至少两个平行布置的锁定料斗，每个锁定料斗连接到下游气相聚合反应器。

    FLUIDIZED BED REACTOR AND METHOD FOR CONVERTING OXYGENATES TO OLEFINS
    9.
    发明公开
    FLUIDIZED BED REACTOR AND METHOD FOR CONVERTING OXYGENATES TO OLEFINS 审中-公开
    WIRBELSCHICHTREAKTOR UND VERFAHREN ZUR UMWANDLUNG VON SAUERSTOFFVERBINDUNGEN OLEFINE

    公开(公告)号：EP2719451A1

    公开(公告)日：2014-04-16

    申请号：EP12797214.9

    申请日：2012-05-30

    申请人： Fude (Beijing) Chemical & Industry Co., Ltd ,  Tsinghua University

    发明人： WEI, Fei ,  WEI, Xiaobo ,  WANG, Yao ,  ZHU, Chang

    IPC分类号： B01J8/24 ,  C07C1/20 ,  C07C11/02

    CPC分类号： C07C1/22 ,  B01J8/0055 ,  B01J8/1836 ,  B01J8/1863 ,  B01J8/24 ,  B01J8/28 ,  C07C1/20 ,  C07C2529/85 ,  Y02P20/584 ,  C07C11/02

    摘要： The present invention provides a fluidized bed reactor and its use for producing olefins from oxygenates, the fluidized bed reactor comprises: a reaction zone located in the lower portion of the fluidized bed reactor and comprising a lower dense phase zone and an upper riser, wherein the dense phase zone and the riser are connected with each other transitionally; a separation zone located in the upper portion of the fluidized bed reactor and comprising a settling chamber, a fast gas-solid separation means, a cyclone and a gas collecting chamber, wherein the riser extends upwardly into the separation zone and is connected at its outlet with the inlet of the fast gas-solid separation means, the fast gas-solid separation means is connected at its outlet with the inlet of the cyclone via a fast gas passage, the cyclone is connected at its outlet with the gas collecting chamber, and the gas collecting chamber is located below the reactor outlet and connected therewith; and a catalyst recycle line for recycling the catalyst from the settling chamber back to the dense phase zone, a catalyst withdrawl line for withdrawing the deactivated catalyst from the settling chamber and/or the dense phase zone to the catalyst regeneration means, and a catalyst return line for returning the regenerated catalyst from the catalyst regeneration means to the dense phase zone.

    摘要翻译： 本发明提供一种流化床反应器及其用于从含氧化合物生产烯烃的用途，该流化床反应器包括：反应区，位于流化床反应器的下部，并包含下部致密相区和上部提升管，其中 密相区和提升管相互连接; 位于流化床反应器上部的分离区，包括沉降室，快速气固分离装置，旋风分离器和气体收集室，其中提升管向上延伸进入分离区并连接在其出口 随着快速气固分离装置的入口，快速气固分离装置通过快速气体通道在其出口与旋风分离器的入口连接，旋风分离器在其出口与气体收集室连接， 气体收集室位于反应器出口下方并与之连接; 以及用于将催化剂从沉降室再循环回密相区域的催化剂再循环管线，用于将去活化催化剂从沉降室和/或致密相区域抽出到催化剂再生装置的催化剂提取管线，以及催化剂返回 使再生催化剂从催化剂再生装置返回到致密相区。