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    Apparatus and process for mixing fluids
    91.
    发明公开
    Apparatus and process for mixing fluids 失效
    Apparat und Verfahren zum Mischen vonFlüssigkeiten。

    公开(公告)号：EP0239171A2

    公开(公告)日：1987-09-30

    申请号：EP87200521.0

    申请日：1987-03-20

    申请人： SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.

    发明人： Barnes, Peter Haddon

    IPC分类号： B01F5/04 ,  B01J8/24

    CPC分类号： C10G11/18 ,  B01F5/0405 ,  B01J8/1827

    摘要： Apparatus for mixing fluids (e.g. liquid hydrocarbons and steam) comprising a tubular mixing section having in its upstream end part an annular inlet opening (2) for a first fluid defined inside substantially coaxially arranged inlet means (7) for a second fluid and an outlet opening for a fluid mixture.
    The invention further relates to a process for mixing fluids (e.g. for use in catalytic cracking of hydrocarbonaceous material).

    摘要翻译： 用于混合流体（例如液体烃和蒸汽）的装置，其包括管状混合部分，其在其上游端部分具有用于第一流体的环形入口（2），所述第一流体限定在基本同轴布置的入口装置（7）内部，用于第二流体和出口 打开流体混合物。 本发明还涉及用于混合流体（例如用于烃类材料的催化裂化）的方法。

    Improvements in fluidized bed polymerization reactors
    92.
    发明公开
    Improvements in fluidized bed polymerization reactors 失效
    流化床聚合反应器的改进

    公开(公告)号：EP0173261A2

    公开(公告)日：1986-03-05

    申请号：EP85110605.4

    申请日：1985-08-23

    申请人： UNION CARBIDE CORPORATION

    发明人： Rhee, Seung Joon ,  Simpson, Larry Lee

    IPC分类号： B01J8/24 ,  B01J8/44

    CPC分类号： B01J8/1827 ,  B01J8/44 ,  B01J2208/00256 ,  B01J2208/00274 ,  C08F10/00 ,  C08F2/01 ,  C08F2/34

    摘要： A fluidized bed reactor and operating process is disclosed, the reactor including distributor plate means to provide distribution of fluid passing upwardly into a fluidized bed; mixing chamber positioned below the distributor plate neans; fluid entry means, preferably at the base of the reactor, or the passage of fluid into the reactor; flow deflector means issociated with the entry means for providing at least an up- vardly fluid flow path and an outward fluid flow path along the vall of the mixing chamber to inhibit the accumulation of solids ind liquid in the mixing chamber.

    摘要翻译： 公开了一种流化床反应器和操作方法，所述反应器包括分布板装置以提供向上流入流化床的流体分布; 位于分配板下方的混合室; 流体进入装置，优选在反应器底部或流体进入反应器; 与入口装置相连的流动偏转器装置，用于提供至少一个沿混合室的凸缘的向上的流体流动路径和向外的流体流动路径，以防止固体在混合室内积聚液体。

    CONTINUOUS GAS FLUIDIZED BED POLYMERIZATION PROCESS
    100.
    发明公开
    CONTINUOUS GAS FLUIDIZED BED POLYMERIZATION PROCESS 审中-公开
    连续气体流化床聚合工艺

    公开(公告)号：EP3274375A1

    公开(公告)日：2018-01-31

    申请号：EP16713828.8

    申请日：2016-03-24

    申请人： SABIC Global Technologies B.V.

    发明人： ALTHUKAIR, Mohammed ,  ASHRI, Abdulrahman

    IPC分类号： C08F2/34 ,  C08F2/01 ,  B01J8/20 ,  B01J19/18

    CPC分类号： B01J8/0015 ,  B01J8/1827 ,  B01J8/1836 ,  B01J8/20 ,  B01J19/18 ,  B01J2208/00274 ,  B01J2208/003 ,  B01J2219/00006 ,  C08F2/01 ,  C08F2/34 ,  C08F10/02 ,  C08F10/00 ,  C08F210/16 ,  C08F210/08 ,  C08F2500/12

    摘要： The invention relates to a process for the preparation of a polyolefin in a reaction system from one or more α-olefin monomers of which at least one is ethylene or propylene, 5 wherein the reaction system comprises a reactor, a product purge bin, a granular feed bin, wherein the granular feed bin is located downstream of the product purge bin, a recovery unit and an extrusion unit directly coupled to the granular fed bin, wherein the reactor comprises a fluidized bed, an expanded section located at or near the top of the reactor, a distribution plate located at the lower part of the reactor and an 10 inlet for a recycle stream located under the distribution plate, wherein the process comprises a) feeding a polymerization catalyst to the fluidized bed in the area above the distribution plate, b) feeding the one or more α-olefin monomers to the reactor, 15 c) circulating fluids from the top of the reactor to the bottom of the reactor, wherein the circulating fluids are cooled using a heat exchanger, resulting in a cooled recycle stream comprising liquid, and wherein the cooled recycle stream is introduced into the reactor using the inlet for the recycle stream, d) withdrawing a stream comprising the polyolefin and fluids from the reactor and 20 passing said stream into the product purge bin, e) purging the product purge bin with a purge stream comprising a first inert gas, preferably nitrogen and steam such that a stream comprising a purged polyolefin and a stream comprising fluids, wherein the stream comprising the fluids is substantially free of steam, is obtained, 25 f) introducing at least part of the stream comprising the fluids back into the reactor via the recovery unit, g) introducing the stream comprising the purged polyolefin into the granular feed bin and h) contacting a deactivating stream comprising steam with the purged polyolefin in the 30 granular feed bin to obtain a polyolefin that is substantially free of active polymerization catalyst.