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    Catalyst regenerator with a centerwell
    1.
    发明授权
    Catalyst regenerator with a centerwell 有权
    具有中心室的催化剂再生器

    公开(公告)号：US07435331B2

    公开(公告)日：2008-10-14

    申请号：US11599763

    申请日：2006-11-15

    申请人： Robert B. Peterson ,  Chris Santner ,  Michael Tallman

    发明人： Robert B. Peterson ,  Chris Santner ,  Michael Tallman

    IPC分类号： C10G11/00

    CPC分类号： B01J8/1827 ,  B01J8/003 ,  B01J8/1818 ,  B01J2219/00024 ,  C10G11/182

    摘要： A method of converting an original FCC unit of side by side configuration to a converted FCC unit for processing light feedstock by replacing an regenerator in the original FCC unit with an embodied regenerator. From the original FCC unit, the air supply assembly is removed and a centerwell is installed with a fluidization gas, fuel, and air inlet(s) through the centerwell. Distribution rings are connected to each of fluidization gas and fuel inlet(s). An internal pipe and a standpipe portion are installed, wherein a lower end of the standpipe extends into the centerwell creating a radial slot, and wherein the lower end of the standpipe is spaced above the deflector plate in the centerwell to allow flow of spent catalyst through the standpipe and provide deflection of the spent catalyst flow for mixing the spent catalyst with fuel oil that is vaporized within the centerwell.

    摘要翻译： 将具有并排配置的原始FCC单元转换为用于处理光进料的转换FCC单元的方法，通过用具体的再生器代替原始FCC单元中的再生器。 从原来的FCC装置中，空气供应组件被移除，并且中心室安装有通过中心井的流化气体，燃料和空气入口。 分配环连接到流化气体和燃料入口中的每一个。 安装内管和立管部分，其中立管的下端延伸到中心井中，形成径向槽，并且其中竖管的下端在中心室中间隔开偏转板的上方，以允许废催化剂流过 立管并且提供废催化剂流的偏转以将废催化剂与在中心室内蒸发的燃料油混合。

    Catalyst regenerator with a centerwell
    2.
    发明授权
    Catalyst regenerator with a centerwell 有权
    具有中心室的催化剂再生器

    公开(公告)号：US07153479B2

    公开(公告)日：2006-12-26

    申请号：US10065376

    申请日：2002-10-10

    申请人： Robert B. Peterson ,  Chris Santner ,  Michael Tallman

    发明人： Robert B. Peterson ,  Chris Santner ,  Michael Tallman

    IPC分类号： B01J8/18 ,  B01J8/24 ,  B01J8/26 ,  C10G11/18 ,  C10G9/32

    CPC分类号： B01J8/1827 ,  B01J8/003 ,  B01J8/1818 ,  B01J2219/00024 ,  C10G11/182

    摘要： A catalyst regenerator for regenerating spent light FCC catalyst and heating the catalyst to supply heat to an FCC reactor. The regenerator has discharge outlets for catalyst and off gas and a valve for introducing spent catalyst through a central stand pipe portion. The regenerator houses a dense phase catalyst bed. A centerwell receives a lower end of the standpipe portion and defines an annulus therebetween. The spent catalyst is introduced through the standpipe portion into the annulus. A fuel distributor introduces fuel into the centerwell for mixing with the catalyst in the annulus. A fluidization distributor introduces fluidization gas into the centerwell for fluidizing the catalyst in the annulus. A radial slot in the centerwell introduces the catalyst and fuel mixture from the annulus below the upper surface of the dense phase bed. An air distributor located below the radial slot introduces combustion air into the dense phase bed.

    摘要翻译： 用于再生废光FCC催化剂并加热催化剂以向FCC反应器供应热量的催化剂再生器。 再生器具有用于催化剂和废气的排出口，以及用于通过中央立管部引入废催化剂的阀。 再生器容纳密相催化剂床。 中心井容纳立管部分的下端，并在其间限定一个环形空间。 废催化剂通过立管部分引入环形空间。 燃料分配器将燃料引入中心室以与环空中的催化剂混合。 流化分配器将流化气体引入中心室，以使环中的催化剂流化。 中心井的径向槽将催化剂和燃料混合物从密相床上表面下方的环带引入。 位于径向槽下方的空气分配器将燃烧空气引入密相床。

    Catalyst regenerator with a centerwell
    3.
    发明申请
    Catalyst regenerator with a centerwell 有权
    具有中心室的催化剂再生器

    公开(公告)号：US20070051666A1

    公开(公告)日：2007-03-08

    申请号：US11599763

    申请日：2006-11-15

    申请人： Robert Peterson ,  Chris Santner ,  Michael Tallman

    发明人： Robert Peterson ,  Chris Santner ,  Michael Tallman

    IPC分类号： C10G47/24 ,  C10G47/02

    CPC分类号： B01J8/1827 ,  B01J8/003 ,  B01J8/1818 ,  B01J2219/00024 ,  C10G11/182

    摘要： A method of converting an original FCC unit of side by side configuration to a converted FCC unit for processing light feedstock by replacing an regenerator in the original FCC unit with an embodied regenerator. From the original FCC unit, the air supply assembly is removed and a centerwell is installed with a fluidization gas, fuel, and air inlet(s) through the centerwell. Distribution rings are connected to each of fluidization gas and fuel inlet(s). An internal pipe and a standpipe portion are installed, wherein a lower end of the standpipe extends into the centerwell creating a radial slot, and wherein the lower end of the standpipe is spaced above the deflector plate in the centerwell to allow flow of spent catalyst through the standpipe and provide deflection of the spent catalyst flow for mixing the spent catalyst with fuel oil that is vaporized within the centerwell.

    摘要翻译： 将具有并排配置的原始FCC单元转换为用于处理光进料的转换FCC单元的方法，通过用具体的再生器代替原始FCC单元中的再生器。 从原来的FCC装置中，空气供应组件被移除，并且中心室安装有通过中心井的流化气体，燃料和空气入口。 分配环连接到流化气体和燃料入口中的每一个。 安装内管和立管部分，其中立管的下端延伸到中心井中，形成径向槽，并且其中竖管的下端在中心室中间隔开偏转板的上方，以允许废催化剂流过 立管并且提供废催化剂流的偏转以将废催化剂与在中心室内蒸发的燃料油混合。

    INTEGRATED CATALYTIC CRACKING AND STEAM PYROLYSIS PROCESS FOR OLEFINS
    4.
    发明申请
    INTEGRATED CATALYTIC CRACKING AND STEAM PYROLYSIS PROCESS FOR OLEFINS 有权
    综合催化裂化和汽油热解过程

    公开(公告)号：US20050150817A1

    公开(公告)日：2005-07-14

    申请号：US10707817

    申请日：2004-01-14

    申请人： Michael Tallman ,  Chris Santner ,  Richard Miller

    发明人： Michael Tallman ,  Chris Santner ,  Richard Miller

    IPC分类号： C10G69/06 ,  C10G9/36 ,  C10G11/14 ,  C10G11/18 ,  C10G21/00 ,  C10G27/06 ,  C10G45/00 ,  C10G51/06 ,  C10G69/04

    CPC分类号： C10G51/06 ,  C10G2400/20

    摘要： Integration of gas oil and light olefin catalytic cracking zones with a pyrolytic cracking zone to maximize efficient production of petrochemicals is disclosed. Integration of the units in parallel allows production of an overall product stream with maximum ethylene and/or propylene by routing various feedstreams and recycle streams to the appropriate cracking zone(s), e.g. ethane/propane to the steam pyrolysis zone and C4 C6 olefins to the light olefin cracking zone. This integration enhances the value of the material balances produced by the integrated units.

    摘要翻译： 公开了瓦斯油和轻质烯烃催化裂化区与热解裂化区的集成，以最大化石油化工产品的有效生产。 平行整合单元允许通过将各种进料流和再循环流布置到适当的裂化区，例如，将最终的乙烯和/或丙烯生成总产物流。 乙烷/丙烷至蒸气热解区和C 4 C 6 C 6烯烃至轻烯烃裂化区。 这种一体化增强了综合单位产生的物料平衡价值。

    Integrated catalytic cracking and steam pyrolysis process for olefins
    5.
    发明授权
    Integrated catalytic cracking and steam pyrolysis process for olefins 有权
    用于烯烃的综合催化裂化和蒸汽热解过程

    公开(公告)号：US07128827B2

    公开(公告)日：2006-10-31

    申请号：US10707817

    申请日：2004-01-14

    申请人： Michael J. Tallman ,  Chris Santner ,  Richard B. Miller

    发明人： Michael J. Tallman ,  Chris Santner ,  Richard B. Miller

    IPC分类号： C10G53/16 ,  C07C4/04 ,  C07C4/06

    CPC分类号： C10G51/06 ,  C10G2400/20

    摘要： Integration of gas oil and light olefin catalytic cracking zones with a pyrolytic cracking zone to maximize efficient production of petrochemicals is disclosed. Integration of the units in parallel allows production of an overall product stream with maximum ethylene and/or propylene by routing various feedstreams and recycle streams to the appropriate cracking zone(s), e.g. ethane/propane to the steam pyrolysis zone and C4 C6 olefins to the light olefin cracking zone. This integration enhances the value of the material balances produced by the integrated units.

    摘要翻译： 公开了瓦斯油和轻质烯烃催化裂化区与热解裂化区的集成，以最大化石油化工产品的有效生产。 平行整合单元允许通过将各种进料流和再循环流布置到适当的裂化区，例如，将最终的乙烯和/或丙烯生成总产物流。 乙烷/丙烷至蒸气热解区和C 4 C 6 C 6烯烃至轻烯烃裂化区。 这种一体化增强了综合单位产生的物料平衡价值。