Multistage reaction system with interstage sparger systems
    1.
    发明授权
    Multistage reaction system with interstage sparger systems 失效
    具有级间分布器系统的多级反应系统

    公开(公告)号:US07060863B2

    公开(公告)日:2006-06-13

    申请号:US10302250

    申请日:2002-11-22

    IPC分类号: C07C2/66

    摘要: A process and system for the vapor phase alkylation of an aromatic substrate in a multi-stage alkylation reaction zone having a plurality of series-connected catalyst beds spaced from one another to provide mixing zones between adjacent catalyst beds. A feedstock containing an aromatic substrate and a C2–C4 alkylating agent is supplied to an inlet side of the reaction zone. The reaction zone is operated at conditions in which the aromatic substrate is in the gas phase and causing vapor phase alkylation of the aromatic substrate as the aromatic substrate and the alkylating agent flow through the reaction zone and pass from one catalyst bed to the next. A quench fluid comprising one or both of the aromatic substrate and the alkylating agent is supplied into the interior of the mixing zone through a plurality of flow paths in which one portion of the flow paths is directed upwardly within the mixing zone and another portion downwardly within the mixing zone. Alkylated product is then recovered from the downstream side of the reaction zone. The quench fluid is supplied to the mixing zone through a plurality of dispersion channels which are spaced laterally from one another and extend transversely across the mixing chamber. At least some of the dispersion channels dispense the quench fluid alternately, upwardly and downwardly within the mixing zone.

    摘要翻译: 一种用于在多级烷基化反应区中芳族底物气相烷基化的方法和系统,其具有彼此间隔开的多个串联的催化剂床,以在相邻的催化剂床之间提供混合区。 将含有芳族底物和C 2 -C 4烷基化剂的原料供给到反应区的入口侧。 反应区域在芳香族基质处于气相的条件下进行,芳香族基质作为芳香族基质进行气相烷基化,烷基化剂流过反应区,从一个催化剂床到另一个催化剂床。 包含芳族底物和烷基化剂中的一种或两种的骤冷流体通过多个流动路径供应到混合区的内部,其中流动路径的一部分在混合区域内向上指向, 混合区。 然后从反应区的下游侧回收烷基化产物。 骤冷流体通过多个分散通道供应到混合区域,这些分散通道彼此横向间隔开并横向跨越混合室。 至少一些分散通道在混合区内交替地向上和向下分配骤冷流体。

    Multistage reaction system with interstage sparger systems
    2.
    发明授权
    Multistage reaction system with interstage sparger systems 失效
    具有级间分布器系统的多级反应系统

    公开(公告)号:US06486371B1

    公开(公告)日:2002-11-26

    申请号:US09723650

    申请日:2000-11-28

    IPC分类号: C07C266

    摘要: Vapor phase alkylation of an aromatic substrate in a multi-stage alkylation reaction zone having a plurality of series-connected catalyst beds providing mixing zones between adjacent catalyst beds. An aromatic substrate and a C2-C4 alkylating agent is supplied to an inlet side of a gas phase reaction zone causing vapor phase alkylation of the aromatic substrate as the aromatic substrate and the alkylating agent flow through the reaction zone from one catalyst bed to the next. A quench fluid comprising one or both of the aromatic substrate and the alkylating agent is supplied into the interior of the mixing zone through a plurality of flow paths. One portion of the flow paths is directed upwardly and another portion downwardly within the mixing zone. The quench fluid is supplied to the mixing zone through a plurality of dispersion channels spaced laterally from one another.

    摘要翻译: 在具有多个串联连接的催化剂床的多级烷基化反应区中芳族底物的气相烷基化提供相邻催化剂床之间的混合区。 将芳香族基质和C 2〜C 4烷基化剂供给到气相反应区的入口侧,引起作为芳香族底物的芳香族基质的气相烷基化,烷基化剂从一个催化剂床流到下一个催化剂床 。 包含芳族底物和烷基化剂中的一种或两种的骤冷流体通过多个流动路径被供给到混合区的内部。 流动路径的一部分向上引导,另一部分在混合区域内向下引导。 骤冷流体通过彼此横向隔开的多个分散通道供应到混合区域。

    Process for recycling product streams separated from a hydrocarbon-containing feed stream
    3.
    发明授权
    Process for recycling product streams separated from a hydrocarbon-containing feed stream 有权
    用于回收与含烃进料流分离的产物流的方法

    公开(公告)号:US08883918B2

    公开(公告)日:2014-11-11

    申请号:US13392531

    申请日:2010-09-10

    摘要: The present invention relates to a process for recycling product streams that have been separated from a hydrocarbon-containing feed stream comprising olefin monomer, olefin co-monomer, hydrocarbon diluent and components such as H2, N2, O2, CO, CO2, and formaldehyde. In accordance with the present process a hydrocarbon-containing feed stream is separated into a) a first side stream comprising hydrocarbon diluent and olefin monomer; b) a second side stream which is substantially hydrogen-free and comprises hydrocarbon diluent and olefin monomer, c) a bottom stream comprising substantially olefin-free hydrocarbon diluent, and d) an overhead vapor stream comprising olefin monomer, hydrocarbon diluent and components such as formaldehyde, H2, N2, O2, CO and CO2. The present process further includes recycling said first and said second side streams in a polymerization process for preparing bimodal polyolefin.

    摘要翻译: 本发明涉及一种从包含烯烃单体,烯烃共聚单体,烃稀释剂和诸如H 2,N 2,O 2,CO,CO 2和甲醛的组分的含烃进料流中分离的产物流的方法。 根据本发明方法,将含烃进料流分离为a)包含烃稀释剂和烯烃单体的第一侧流; b)基本上无氢的第二侧流,包括烃稀释剂和烯烃单体,c)包含基本上不含烃的烃稀释剂的底部料流,和d)包含烯烃单体,烃稀释剂和组分如 甲醛,H2,N2,O2,CO和CO2。 本方法还包括在用于制备双峰聚烯烃的聚合方法中回收所述第一和第二侧流。

    Process for the separation of a hydrocarbon-containing feed stream
    4.
    发明授权
    Process for the separation of a hydrocarbon-containing feed stream 有权
    用于分离含烃进料流的方法

    公开(公告)号:US08557087B2

    公开(公告)日:2013-10-15

    申请号:US12669132

    申请日:2008-07-15

    申请人: Denis Mignon

    发明人: Denis Mignon

    摘要: The present invention relates to a process for the separation by distillation of a hydrocarbon-containing feed stream containing olefin monomer, co-monomer and hydrocarbon diluent. The present invention also relates to a distillation system including a distillation column for carrying out the process according to the invention.

    摘要翻译: 本发明涉及一种通过蒸馏分离含有烯烃单体,共聚单体和烃类稀释剂的含烃进料流的方法。 本发明还涉及包括用于实施本发明方法的蒸馏塔的蒸馏系统。

    PROCESS FOR RECYCLING PRODUCT STREAMS SEPARATED FROM A HYDROCARBON-CONTAINING FEED STREAM
    5.
    发明申请
    PROCESS FOR RECYCLING PRODUCT STREAMS SEPARATED FROM A HYDROCARBON-CONTAINING FEED STREAM 有权
    回收含有含油料进料流的产品流程的方法

    公开(公告)号:US20120178879A1

    公开(公告)日:2012-07-12

    申请号:US13392531

    申请日:2010-09-10

    IPC分类号: C08L23/02 B01J19/00

    摘要: The present invention relates to a process for recycling product streams that have been separated from a hydrocarbon-containing feed stream comprising olefin monomer, olefin co-monomer, hydrocarbon diluent and components such as H2, N2, O2, CO, CO2, and formaldehyde. In accordance with the present process a hydrocarbon-containing feed stream is separated into a) a first side stream comprising hydrocarbon diluent and olefin monomer; b) a second side stream which is substantially hydrogen-free and comprises hydrocarbon diluent and olefin monomer, c) a bottom stream comprising substantially olefin-free hydrocarbon diluent, and d) an overhead vapor stream comprising olefin monomer, hydrocarbon diluent and components such as formaldehyde, H2, N2, O2, CO and CO2. The present process further includes recycling said first and said second side streams in a polymerization process for preparing bimodal polyolefin.

    摘要翻译: 本发明涉及一种从包含烯烃单体,烯烃共聚单体,烃稀释剂和诸如H 2,N 2,O 2,CO,CO 2和甲醛的组分的含烃进料流中分离的产物流的方法。 根据本发明方法,将含烃进料流分离为a)包含烃稀释剂和烯烃单体的第一侧流; b)基本上无氢的第二侧流,包括烃稀释剂和烯烃单体,c)包含基本上不含烃的烃稀释剂的底部料流,和d)包含烯烃单体,烃稀释剂和组分如 甲醛,H2,N2,O2,CO和CO2。 本方法还包括在用于制备双峰聚烯烃的聚合方法中回收所述第一和第二侧流。

    Process for the Separation of a Hydrocarbon-Containing Feed Stream
    6.
    发明申请
    Process for the Separation of a Hydrocarbon-Containing Feed Stream 有权
    用于分离含烃载体原料流的方法

    公开(公告)号:US20100264014A1

    公开(公告)日:2010-10-21

    申请号:US12669132

    申请日:2008-07-15

    申请人: Denis Mignon

    发明人: Denis Mignon

    IPC分类号: B01D3/42 G05D7/00 G05D9/00

    摘要: The present invention relates to a process for the separation by distillation of a hydrocarbon-containing feed stream comprising olefin monomer, co-monomer and hydrocarbon diluent. The present invention also relates to a distillation system comprising a distillation column for carrying out the process according to the invention.

    摘要翻译: 本发明涉及通过蒸馏分离含有烯烃单体,共聚单体和烃稀释剂的含烃进料流的方法。 本发明还涉及包含用于实施本发明方法的蒸馏塔的蒸馏系统。