Apparatus for dehydrogenation of ethylbenzene to styrene
    1.
    发明申请
    Apparatus for dehydrogenation of ethylbenzene to styrene 失效
    乙苯脱氢成苯乙烯的装置

    公开(公告)号:US20070270622A1

    公开(公告)日:2007-11-22

    申请号:US10816297

    申请日:2004-04-01

    Abstract: The present invention discloses a process and apparatus for improving the catalyst life and efficiency in a gas flow catalyst bed reactor assembly. The reactor comprises an outer reaction vessel, an inner displacement cylinder, and an annular catalyst bed surrounding the displacement cylinder having a top half and a bottom half. Fluid flow improvement is achieved by adding at least one baffle to the top half of the displacement cylinder to improve uniformity of fluid flow in the reaction vessel and across the catalyst bed. Also disclosed is a process for improving fluid flow uniformity in a gas phase reactor comprising an outer reaction vessel, an inner displacement vessel having a top half and a bottom half and a reaction outer surface and an inert inner space, and an annular catalyst bed. The process comprises conducting fluid flow simulations using actual reactor conditions. During simulation, baffles are added on the outer reaction surface of the displacement reactor to improve simulated fluid flow. The baffles are added to the displacement cylinder by entering the inner inert space of the cylinder and attaching the baffles to the reaction outer surface from the inner inert space. The process allows the modification of existing reactors without disassembling the reactor.

    Abstract translation: 本发明公开了一种改善气流催化剂床反应器组件的催化剂寿命和效率的方法和装置。 反应器包括外反应容器,内排量圆筒和围绕位移圆筒的环形催化剂床,其具有上半部和下半部。 通过将至少一个挡板添加到排量缸的上半部分来实现流体流动改善,以改善反应容器中和穿过催化剂床的流体流动的均匀性。 还公开了一种用于改善气相反应器中的流体流动均匀性的方法,其包括外部反应容器,具有上半部分和下半部分的内部容积容器以及反应外表面和惰性内部空间以及环形催化剂床。 该方法包括使用实际的反应器条件进行流体流动模拟。 在模拟期间,挡板被添加到位移反应器的外部反应表面上以改善模拟的流体流动。 挡板通过进入气缸的内部惰性空间并将挡板从内部惰性空间连接到反作用外表面而被添加到排量缸中。 该方法允许在不拆卸反应器的情况下修改现有反应器。

    Apparatus for dehydrogenation of ethylbenzene to styrene and method of retrofitting the apparatus
    2.
    发明授权
    Apparatus for dehydrogenation of ethylbenzene to styrene and method of retrofitting the apparatus 失效
    乙苯脱氢成苯乙烯的装置及改装方法

    公开(公告)号:US07459132B2

    公开(公告)日:2008-12-02

    申请号:US10816297

    申请日:2004-04-01

    Abstract: The present invention discloses a process and apparatus for improving the catalyst life and efficiency in a gas flow catalyst bed reactor assembly. The reactor comprises an outer reaction vessel, an inner displacement cylinder, and an annular catalyst bed surrounding the displacement cylinder having a top half and a bottom half. Fluid flow improvement is achieved by adding at least one baffle to the top half of the displacement cylinder to improve uniformity of fluid flow in the reaction vessel and across the catalyst bed. Also disclosed is a process for improving fluid flow uniformity in a gas phase reactor comprising an outer reaction vessel, an inner displacement vessel having a top half and a bottom half and a reaction outer surface and an inert inner space, and an annular catalyst bed. The process comprises conducting fluid flow simulations using actual reactor conditions. During simulation, baffles are added on the outer reaction surface of the displacement reactor to improve simulated fluid flow. The baffles are added to the displacement cylinder by entering the inner inert space of the cylinder and attaching the baffles to the reaction outer surface from the inner inert space. The process allows the modification of existing reactors without disassembling the reactor.

    Abstract translation: 本发明公开了一种改善气流催化剂床反应器组件的催化剂寿命和效率的方法和装置。 反应器包括外反应容器,内排量圆筒和围绕位移圆筒的环形催化剂床,其具有上半部和下半部。 通过将至少一个挡板添加到排量缸的上半部分来实现流体流动改善,以改善反应容器中和穿过催化剂床的流体流动的均匀性。 还公开了一种用于改善气相反应器中的流体流动均匀性的方法,其包括外部反应容器,具有上半部分和下半部分的内部容积容器以及反应外表面和惰性内部空间以及环形催化剂床。 该方法包括使用实际的反应器条件进行流体流动模拟。 在模拟期间,挡板被添加到位移反应器的外部反应表面上以改善模拟的流体流动。 挡板通过进入气缸的内部惰性空间并将挡板从内部惰性空间连接到反作用外表面而被添加到排量缸中。 该方法允许在不拆卸反应器的情况下修改现有反应器。

    Apparatus for dehydrogenation of ethylbenzene to styrene
    3.
    发明授权
    Apparatus for dehydrogenation of ethylbenzene to styrene 失效
    乙苯脱氢成苯乙烯的装置

    公开(公告)号:US06762335B1

    公开(公告)日:2004-07-13

    申请号:US09515314

    申请日:2000-02-29

    Abstract: The present invention discloses a process and apparatus for improving the catalyst life and efficiency in a gas flow catalyst bed reactor assembly. The reactor comprises an outer reaction vessel, an inner displacement cylinder, and an annular catalyst bed surrounding the displacement cylinder having a top half and a bottom half. Fluid flow improvement is achieved by adding at least one baffle to the top half of the displacement cylinder to improve uniformity of fluid flow in the reaction vessel and across the catalyst bed. Also disclosed is a process for improving fluid flow uniformity in a gas phase reactor comprising an outer reaction vessel, an inner displacement vessel having a top half and a bottom half and a reaction outer surface and an inert inner space, and an annular catalyst bed. The process comprises conducting fluid flow simulations using actual reactor conditions. During simulation, baffles are added on the outer reaction surface of the displacement reactor to improve simulated fluid flow. The baffles are added to the displacement cylinder by entering the inner inert space of the cylinder and attaching the baffles to the reaction outer surface from the inner inert space. The process allows the modification of existing reactors without disassembling the reactor.

    Abstract translation: 本发明公开了一种改善气流催化剂床反应器组件的催化剂寿命和效率的方法和装置。 反应器包括外反应容器,内排量圆筒和围绕位移圆筒的环形催化剂床,其具有上半部和下半部。 通过将至少一个挡板添加到排量缸的上半部分来实现流体流动改善,以改善反应容器中和穿过催化剂床的流体流动的均匀性。 还公开了一种用于改善气相反应器中的流体流动均匀性的方法,其包括外部反应容器,具有上半部分和下半部分的内部容积容器以及反应外表面和惰性内部空间以及环形催化剂床。 该方法包括使用实际的反应器条件进行流体流动模拟。 在模拟期间,挡板被添加到位移反应器的外部反应表面上以改善模拟的流体流动。 挡板通过进入气缸的内部惰性空间并将挡板从内部惰性空间连接到反作用外表面而被添加到排量缸中。 该方法允许在不拆卸反应器的情况下修改现有反应器。

    Heat integration in alkylation/transalkylation process
    4.
    发明授权
    Heat integration in alkylation/transalkylation process 失效
    在烷基化/烷基转移过程中的热积分

    公开(公告)号:US5900518A

    公开(公告)日:1999-05-04

    申请号:US739897

    申请日:1996-10-30

    CPC classification number: C07C15/02 C07C2529/06 Y02P20/582

    Abstract: The present invention addresses heat integration in an alkylation/transalkylation process involving alkylation of an aromatic substrate with a C.sub.2 -C.sub.4 alklating agent coupled with separation to recover a monoalkylated aromatic product and liquid phase transalkylation of a polyalkylated product. Aromatic feedstock and a C.sub.2 -C.sub.4 alkylating agent are supplied to an alkylation reaction zone which is operated to produce an alkylated product. The output from the alkylation reaction zone initially travels through an arrangement of heat exchangers. From there, the alkylation effluent passes into the first separation zone which is operated to produce a lower boiling fraction comprising the aromatic substrate, which may be recycled to the alkylation reaction zone, and a higher boiling fraction comprising a mixture of monoalkylated and polyalkylated aromatics. This lower boiling fraction first travels back through portions of the heat exchanger arrangement on the way to recycle into the alkylation zone. The higher boiling fraction of the first separation zone is supplied to a secondary separation zone to produce a second lower boiling fraction comprising the desired monoalkylated product and a higher boiling fraction comprising polyalkylated product. At least a portion of the higher boiling polyalkylated fraction passes through a portion of the heat exchanger arrangement into a transalkylation reaction zone containing a molecular sieve transalkylation catalyst operated under liquid phase conditions to cause disproportionation of the polyalkylated fraction to arrive at a disproportionation product having a reduced polyalkylated aromatic content and an enhanced monoalkylated aromatic content.

    Abstract translation: 本发明涉及烷基化/烷基转移方法中的热积分,其涉及通过与分离相结合的C2-C4烷基化剂芳族底物的烷基化以回收单烷基化芳族产物和多烷基化产物的液相烷基转移。 将芳族原料和C 2 -C 4烷基化剂供给到烷基化反应区,其操作以产生烷基化产物。 烷基化反应区的输出最初通过热交换器的排列。 从那里,烷基化流出物进入第一分离区,其被操作以产生包含可以再循环到烷基化反应区的芳族底物的较低沸点馏分,以及包含单烷基化和多烷基化芳族化合物的混合物的较高沸点馏分。 该低沸点馏分首先通过热交换器装置的一部分在回收进入烷基化区的路上返回。 将第一分离区的较高沸点馏分供应到第二分离区以产生包含所需单烷基化产物和包含多烷基化产物的较高沸点馏分的第二较低沸点馏分。 高沸点多烷基化馏分的至少一部分通过热交换器装置的一部分进入含烷基转移反应区的烷基转移反应区,该烷基转移反应区含有在液相条件下操作的分子筛烷基转移催化剂,导致多烷基化馏分的歧化,得到具有 减少的多烷基化芳族含量和增强的单烷基化芳族含量。

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