Methods and apparatuses for separating toluene from multiple hydrocarbon streams
    1.
    发明授权
    Methods and apparatuses for separating toluene from multiple hydrocarbon streams 有权
    从多个烃流中分离甲苯的方法和装置

    公开(公告)号:US08716545B1

    公开(公告)日:2014-05-06

    申请号:US13712714

    申请日:2012-12-12

    Applicant: UOP LLC

    Abstract: Methods and apparatuses for separating toluene from multiple hydrocarbon streams are provided. A method includes fractionating a first hydrocarbon stream, which includes benzene-depleted fractionation bottoms from benzene fractionation, in a first fractionation zone into a first fractionation overhead stream that includes toluene and a first fractionation bottoms. A second hydrocarbon stream, which includes toluene and is substantially free of compounds having a higher vapor pressure than toluene, is fractionated in a second fractionation zone into a second fractionation overhead stream including toluene and a second fractionation bottoms. The second fractionation zone is in liquid isolation from and in vapor communication with the first fractionation zone. The first fractionation bottoms are removed from the first fractionation zone, and the second fractionation bottoms are removed from the second fractionation zone separate from the first fractionation bottoms. The first fractionation overhead stream and the second fractionation overhead stream are combined to produce a combined fractionation overhead stream.

    Abstract translation: 提供了从多个烃流中分离甲苯的方法和装置。 一种方法包括在第一分馏区中将包含苯分馏塔底馏分的第一烃流分馏成包括甲苯和第一分馏塔底馏分的第一分馏塔顶馏出物流。 包含甲苯并且基本上不含具有比甲苯更高的蒸气压的化合物的第二烃流在第二分馏区中分馏成包括甲苯和第二分馏塔底物的第二分馏塔顶物流。 第二分馏区与第一分馏区液体隔离并与其蒸汽连通。 第一分馏塔底物从第一分馏区中除去,第二分馏塔底物从与第一分馏塔分离的第二分馏区域中除去。 组合第一分馏塔顶流和第二分馏塔顶流以产生组合分馏塔顶馏分。

    SPLIT-SHELL FRACTIONATION COLUMNS AND ASSOCIATED PROCESSES FOR SEPARATING AROMATIC HYDROCARBONS
    2.
    发明申请
    SPLIT-SHELL FRACTIONATION COLUMNS AND ASSOCIATED PROCESSES FOR SEPARATING AROMATIC HYDROCARBONS 审中-公开
    分离层分离柱和分离芳烃的相关工艺

    公开(公告)号:US20150041307A1

    公开(公告)日:2015-02-12

    申请号:US14511812

    申请日:2014-10-10

    Applicant: UOP LLC

    CPC classification number: C07C7/04 B01D3/141 B01D3/32

    Abstract: Split-shell fractionation columns and associated processes for separating aromatic hydrocarbons are provided herein. In an embodiment, a split-shell fractionation column includes a housing shell having a first height and a partition having a second height and disposed within the housing shell. The partition includes first and second vertically oriented baffles separated by a gap region, a seal plate connecting top ends of the baffles, a first input port formed to extend through the partition for the introduction of a gas into the gap region, and a first output port formed to extend outwardly from a bottom of the gap region and through the housing shell. The partition defines a first distillation zone and a second distillation zone within the housing shell.

    Abstract translation: 本文提供了分离壳分馏塔和用于分离芳族烃的相关方法。 在一个实施例中,裂壳分级柱包括具有第一高度的壳体壳体和具有第二高度并且设置在壳体壳体内的分隔件。 分隔件包括由间隙区域分开的第一和第二垂直取向的挡板,连接挡板顶端的密封板,形成为延伸穿过隔板以将气体引入间隙区域的第一输入端口,以及第一输出端 端口形成为从间隙区域的底部向外延伸并且通过壳体壳体。 分隔件限定了壳体壳体内的第一蒸馏区和第二蒸馏区。

    Split-shell fractionation columns and associated processes for separating aromatic hydrocarbons
    3.
    发明授权
    Split-shell fractionation columns and associated processes for separating aromatic hydrocarbons 有权
    分离壳分馏柱和分离芳烃的相关方法

    公开(公告)号:US08877014B2

    公开(公告)日:2014-11-04

    申请号:US13715774

    申请日:2012-12-14

    Applicant: UOP LLC

    CPC classification number: C07C7/04 B01D3/141 B01D3/32

    Abstract: Split-shell fractionation columns and associated processes for separating aromatic hydrocarbons. A split-shell fractionation column includes a housing shell having a first height and a partition having a second height and disposed within the housing shell. The partition includes first and second vertically oriented baffles separated by a gap region, a seal plate connecting top ends of the baffles, a first input port formed to extend through the partition for the introduction of a gas into the gap region, and a first output port formed to extend outwardly from a bottom of the gap region and through the housing shell. The partition defines a first distillation zone and a second distillation zone within the housing shell.

    Abstract translation: 分离壳分馏柱和分离芳烃的相关方法。 裂壳分级柱包括具有第一高度的壳体壳体和具有第二高度并且设置在壳体壳体内的隔板。 分隔件包括由间隙区域分开的第一和第二垂直取向的挡板,连接挡板顶端的密封板,形成为延伸穿过隔板以将气体引入间隙区域的第一输入端口,以及第一输出端 端口形成为从间隙区域的底部向外延伸并且通过壳体壳体。 分隔件限定了壳体壳体内的第一蒸馏区和第二蒸馏区。

    SPLIT-SHELL FRACTIONATION COLUMNS AND ASSOCIATED PROCESSES FOR SEPARATING AROMATIC HYDROCARBONS
    4.
    发明申请
    SPLIT-SHELL FRACTIONATION COLUMNS AND ASSOCIATED PROCESSES FOR SEPARATING AROMATIC HYDROCARBONS 有权
    分离层分离柱和分离芳烃的相关工艺

    公开(公告)号:US20140171715A1

    公开(公告)日:2014-06-19

    申请号:US13715774

    申请日:2012-12-14

    Applicant: UOP LLC

    CPC classification number: C07C7/04 B01D3/141 B01D3/32

    Abstract: Split-shell fractionation columns and associated processes for separating aromatic hydrocarbons are provided herein. In an embodiment, a split-shell fractionation column includes a housing shell having a first height and a partition having a second height and disposed within the housing shell. The partition includes first and second vertically oriented baffles separated by a gap region, a seal plate connecting top ends of the baffles, a first input port formed to extend through the partition for the introduction of a gas into the gap region, and a first output port formed to extend outwardly from a bottom of the gap region and through the housing shell. The partition defines a first distillation zone and a second distillation zone within the housing shell.

    Abstract translation: 本文提供了分离壳分馏塔和用于分离芳族烃的相关方法。 在一个实施例中,裂壳分级柱包括具有第一高度的壳体壳体和具有第二高度并且设置在壳体壳体内的分隔件。 分隔件包括由间隙区域分开的第一和第二垂直取向的挡板,连接挡板顶端的密封板,形成为延伸穿过隔板以将气体引入间隙区域的第一输入端口,以及第一输出端 端口形成为从间隙区域的底部向外延伸并且通过壳体壳体。 分隔件限定了壳体壳体内的第一蒸馏区和第二蒸馏区。

    Split-shell fractionation columns and associated processes for separating aromatic hydrocarbons
    5.
    发明授权
    Split-shell fractionation columns and associated processes for separating aromatic hydrocarbons 有权
    分离壳分馏柱和分离芳烃的相关方法

    公开(公告)号:US09517982B2

    公开(公告)日:2016-12-13

    申请号:US14511812

    申请日:2014-10-10

    Applicant: UOP LLC

    CPC classification number: C07C7/04 B01D3/141 B01D3/32

    Abstract: Split-shell fractionation columns and associated processes for separating aromatic hydrocarbons are provided by using, a split-shell fractionation column includes a housing shell having a first height and a partition having a second height and disposed within the housing shell. The partition includes first and second vertically oriented baffles separated by a gap region, a seal plate connecting top ends of the baffles, a first input port formed to extend through the partition for the introduction of a gas into the gap region, and a first output port formed to extend outwardly from a bottom of the gap region and through the housing shell. The partition defines a first distillation zone and a second distillation zone within the housing shell.

    Abstract translation: 分离壳分馏塔和用于分离芳烃的相关方法通过使用分裂壳分馏塔包括具有第一高度的壳体壳体和具有第二高度的分隔件并且设置在壳体壳体内来提供。 分隔件包括由间隙区域分开的第一和第二垂直取向的挡板,连接挡板顶端的密封板,形成为延伸穿过隔板以将气体引入间隙区域的第一输入端口,以及第一输出端 端口形成为从间隙区域的底部向外延伸并且通过壳体壳体。 分隔件限定了壳体壳体内的第一蒸馏区和第二蒸馏区。

    METHODS AND APPARATUSES FOR REFORMING OF HYDROCARBONS INCLUDING RECOVERY OF PRODUCTS USING MIXING DEVICES
    6.
    发明申请
    METHODS AND APPARATUSES FOR REFORMING OF HYDROCARBONS INCLUDING RECOVERY OF PRODUCTS USING MIXING DEVICES 审中-公开
    用于改造烃类的方法和装置,包括使用混合装置恢复产品的方法和装置

    公开(公告)号:US20160115101A1

    公开(公告)日:2016-04-28

    申请号:US14524271

    申请日:2014-10-27

    Applicant: UOP LLC

    Abstract: Embodiments of apparatuses and methods for reforming of hydrocarbons including recovery of products are provided. In one example, an apparatus comprises a separation zone to receive and separate a reforming-zone effluent to form a net gas phase stream and a liquid phase hydrocarbon stream. A compressor receives and compresses the net gas phase stream to form a compressed net gas phase stream. A chiller receives and cools the liquid phase hydrocarbon stream to form a cooled liquid phase hydrocarbon stream. A first mixing device receives and mixes the compressed net gas phase stream and at least a portion of the cooled liquid phase hydrocarbon stream to extract C3/C4 hydrocarbons from the compressed net gas phase stream into the at least the portion of the cooled liquid phase hydrocarbon stream.

    Abstract translation: 提供了包括产物回收的烃类重整装置和方法的实施例。 在一个实例中,设备包括分离区以接收和分离重整区流出物以形成净气相流和液相烃流。 压缩机接收和压缩净气相流以形成压缩的净气相流。 冷却器接收并冷却液相烃流以形成冷却的液相烃流。 第一混合装置接收和混合压缩的净气相物流和至少一部分冷却的液相烃物流,以将C3 / C4烃从压缩的净气相物流提取到冷却的液相烃的至少一部分中 流。

    METHODS AND APPARATUSES FOR SEPARATING DESORBENT FROM MULTIPLE STREAMS
    7.
    发明申请
    METHODS AND APPARATUSES FOR SEPARATING DESORBENT FROM MULTIPLE STREAMS 审中-公开
    用于从多个流分离吸附物的方法和装置

    公开(公告)号:US20140158521A1

    公开(公告)日:2014-06-12

    申请号:US13712697

    申请日:2012-12-12

    Applicant: UOP LLC

    CPC classification number: B01D3/40 B01D3/141

    Abstract: Methods and apparatuses for separating desorbent from an extract stream and a raffinate stream are provided. An exemplary method includes fractionating a first stream in a first fractionation zone into a first fractionation overhead stream and a first fractionation bottom stream. The first stream includes an extract stream including a desorbent from an adsorption zone. A second stream different from the first stream is fractionated in a second fractionation zone into a second fractionation overhead stream and a second fractionation bottom stream. The second fractionation zone is in liquid isolation from and in vapor communication with the first fractionation zone. The second stream includes a raffinate stream including the desorbent from the adsorption zone. The first and second fractionation bottom streams are separately removed from the respective fractionation zones. The first and second fractionation overhead streams are combined to produce a combined fractionation overhead stream that includes the desorbent.

    Abstract translation: 提供了用于从提取物流和萃余液流中分离解吸剂的方法和装置。 示例性方法包括将第一分馏区中的第一流分馏成第一分馏塔顶流和第一分馏塔底流。 第一物流包括包含来自吸附区的解吸剂的萃取流。 与第一流不同的第二物流在第二分馏区中分馏成第二分馏塔顶物流和第二分馏塔底物流。 第二分馏区与第一分馏区液体隔离并与其蒸汽连通。 第二物流包括包含来自吸附区的解吸剂的萃余液流。 第一和第二分馏塔底流分别从相应的分馏区域移出。 组合第一和第二分馏塔顶流以产生包括解吸剂的组合分馏塔顶流。

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