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11 条记录 (耗时 0.015 秒)

    Process for distillation of multicomponent fluid and production of an argon-enriched stream from a cryogenic air separation process
    3.
    发明授权
    Process for distillation of multicomponent fluid and production of an argon-enriched stream from a cryogenic air separation process 有权
    蒸馏多组分流体的方法和从低温空气分离过程产生富氩流

    公开(公告)号：US06240744B1

    公开(公告)日：2001-06-05

    申请号：US09459561

    申请日：1999-12-13

    申请人： Rakesh Agrawal ,  Donn Michael Herron ,  Jung Soo Choe

    发明人： Rakesh Agrawal ,  Donn Michael Herron ,  Jung Soo Choe

    IPC分类号： F25J300

    CPC分类号： F25J3/04703 ,  B01D3/14 ,  B01D3/141 ,  B01D3/146 ,  F25J3/04412 ,  F25J3/04666 ,  F25J3/04678 ,  F25J3/04733 ,  F25J3/04939 ,  F25J2205/60 ,  F25J2205/80 ,  F25J2205/82 ,  F25J2235/58 ,  F25J2245/58 ,  Y10S62/905 ,  Y10S62/924

    摘要： A process separates a multicomponent feed by distillation into at least one stream enriched in the most volatile component, one stream enriched in the least volatile component, and one stream enriched in a component of intermediate volatility. In one embodiment, the process produces an argon-enriched stream from a cryogenic air separation process. The distillation system includes at least one distillation column that produces a nitrogen-enriched stream from the top of the column, an oxygen product stream from the bottom of the column, and an argon-enriched stream from a partitioned section. The geometry of the partitioned section minimizes vapor and liquid distribution, and includes a vertical separating element and an end separating element to isolate the partitioned section from the intermediate distillation section. The equivalent diameter (De) of the partitioned section is at least 60% of the ideal diameter (Di) of the partitioned section, wherein the equivalent diameter is defined as four times the cross sectional flow area enclosed by the vertical separating element divided by the perimeter formed by the vertical separating element, and the ideal diameter (Di) is the diameter of a circle which has the same cross sectional flow area as that cross sectional flow area which is enclosed by the vertical separating element.

    摘要翻译： 一种方法是通过蒸馏将多组分进料分离成富含最易挥发组分的至少一种物流，富含最不易挥发组分的一种物流和富含中等挥发性组分的一种物流。 在一个实施方案中，该方法从低温空气分离过程产生富氩流。 蒸馏系统包括至少一个蒸馏塔，其从塔的顶部产生富氮流，来自塔底的氧产物流和来自分隔区的富氩流。 分隔部分的几何形状使蒸汽和液体分布最小化，并且包括垂直分离元件和端部分离元件以将分隔部分与中间蒸馏部分隔离。 分隔部分的当量直径（De）为分隔部分的理想直径（Di）的至少60％，其中等效直径定义为垂直分离元件所包围的横截面流动面积的四倍 由垂直分离元件形成的周边，理想直径（Di）是与由垂直分离元件包围的横截面积面积相同的横截面积面积的圆的直径。

    System and Method for Sulfur Recovery
    5.
    发明申请
    System and Method for Sulfur Recovery 有权
    硫回收系统和方法

    公开(公告)号：US20110206601A1

    公开(公告)日：2011-08-25

    申请号：US12709745

    申请日：2010-02-22

    申请人： Xianming Jimmy Li ,  Elmo Nasato ,  Jung Soo Choe

    发明人： Xianming Jimmy Li ,  Elmo Nasato ,  Jung Soo Choe

    IPC分类号： C01B17/027 ,  B01J8/04 ,  G05D7/00

    CPC分类号： C01B17/0404 ,  C01B17/0413 ,  C01B17/0452

    摘要： A sulfur recovery system for recovering sulfur from a sulfur plant feed stream including a first sulfur removal system and a second sulfur removal system. The system includes a sulfur plant feed inlet to the first sulfur removal system, the sulfur plant feed inlet being capable of providing a sulfur plant feed stream at a first pressure. One or more oxidizing gas inlets are arranged and disposed to combine at least one oxidizing gas stream with the sulfur plant feed stream to form a combustion gas for combustion in the first sulfur removal system at a second pressure. A flow restriction device is operably configured to control an operating pressure in one or both of the first sulfur removal system and the second sulfur removal system. A gas processing plant and method for recovering sulfur from a sulfur plant feed stream are also disclosed.

    摘要翻译： 一种硫回收系统，用于从包括第一硫去除系统和第二硫去除系统的硫植物进料流中回收硫。 该系统包括第一硫去除系统的硫植物进料入口，硫植物进料入口能够在第一压力下提供硫植物进料流。 一个或多个氧化气体入口被布置和布置成将至少一个氧化气体流与硫植物进料流组合以在第二压力下形成用于在第一硫去除系统中燃烧的燃烧气体。 流量限制装置可操作地构造成控制第一硫去除系统和第二硫去除系统中的一个或两个中的操作压力。 还公开了一种用于从硫植物进料流中回收硫的气体处理设备和方法。

    System to increase capacity of LNG-based liquefier in air separation process
    7.
    发明授权
    System to increase capacity of LNG-based liquefier in air separation process 有权
    在空气分离过程中增加液化天然气液化器的能力

    公开(公告)号：US07712331B2

    公开(公告)日：2010-05-11

    申请号：US11477924

    申请日：2006-06-30

    申请人： Douglas Paul Dee ,  Jung Soo Choe ,  Donn Michael Herron

    发明人： Douglas Paul Dee ,  Jung Soo Choe ,  Donn Michael Herron

    IPC分类号： F25J1/00 ,  F25J3/00 ,  F17C9/02

    CPC分类号： F25J1/0264 ,  F25J1/0015 ,  F25J1/004 ,  F25J1/0224 ,  F25J1/0234 ,  F25J1/0245 ,  F25J1/0292 ,  F25J3/0406 ,  F25J3/04224 ,  F25J3/04266 ,  F25J3/04272 ,  F25J3/04351 ,  F25J3/04412 ,  F25J3/04678 ,  F25J3/04812 ,  F25J3/04969 ,  F25J2210/02 ,  F25J2210/62 ,  F25J2230/08 ,  F25J2230/42 ,  F25J2245/42

    摘要： A system is set forth to increase the capacity of an LNG-based liquefier in a cryogenic air separation unit wherein, in a low production mode, the nitrogen that is fed to the LNG-based liquefier consists only of at least a portion of the high pressure nitrogen from the distillation column system while in a high production mode, a supplemental compressor is used to boost the pressure of at least a portion of the low pressure nitrogen from the distillation column system to create additional (or replacement) feed to the LNG-based liquefier. A key to the present invention is the supplemental compressor and the associated heat exchange equipment is separate and distinct from the LNG-based liquefier. This allows its purchase to be delayed until a capacity increase is actually needed and thus avoid building an oversized liquefier based on a speculative increase in liquid product demand.

    摘要翻译： 提出了一种系统来提高低温空气分离装置中基于液化天然气的液化器的容量，其中在低生产模式中，供给到基于LNG的液化器的氮仅由至少一部分高的 来自蒸馏塔系统的高压氮气在高生产模式下，补充压缩机用于提高来自蒸馏塔系统的至少一部分低压氮气的压力，以产生到LNG- 液化器。 本发明的关键是补充压缩机，并且相关联的热交换设备与基于液化天然气的液化器是独立的和不同的。 这允许其购买被延迟，直到实际需要增加容量，从而避免在液体产品需求的推测性增加的情况下构建过大的液化器。

    System and method for sulfur recovery
    10.
    发明授权
    System and method for sulfur recovery 有权
    硫回收系统和方法

    公开(公告)号：US08236276B2

    公开(公告)日：2012-08-07

    申请号：US12709745

    申请日：2010-02-22

    申请人： Xianming Jimmy Li ,  Elmo Nasato ,  Jung Soo Choe

    发明人： Xianming Jimmy Li ,  Elmo Nasato ,  Jung Soo Choe

    IPC分类号： B01J19/00 ,  C01B17/00

    CPC分类号： C01B17/0404 ,  C01B17/0413 ,  C01B17/0452

    摘要： A sulfur recovery system for recovering sulfur from a sulfur plant feed stream including a first sulfur removal system and a second sulfur removal system. The system includes a sulfur plant feed inlet to the first sulfur removal system, the sulfur plant feed inlet being capable of providing a sulfur plant feed stream at a first pressure. One or more oxidizing gas inlets are arranged and disposed to combine at least one oxidizing gas stream with the sulfur plant feed stream to form a combustion gas for combustion in the first sulfur removal system at a second pressure. A flow restriction device is operably configured to control an operating pressure in one or both of the first sulfur removal system and the second sulfur removal system. A gas processing plant and method for recovering sulfur from a sulfur plant feed stream are also disclosed.

    摘要翻译： 一种硫回收系统，用于从包括第一硫去除系统和第二硫去除系统的硫植物进料流中回收硫。 该系统包括第一硫去除系统的硫植物进料入口，硫植物进料入口能够在第一压力下提供硫植物进料流。 一个或多个氧化气体入口被布置和布置成将至少一个氧化气体流与硫植物进料流组合以在第二压力下形成用于在第一硫去除系统中燃烧的燃烧气体。 流量限制装置可操作地构造成控制第一硫去除系统和第二硫去除系统中的一个或两个中的操作压力。 还公开了一种用于从硫植物进料流中回收硫的气体处理设备和方法。