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127 条记录 (耗时 0.02 秒)

    SEPARATION METHOD AND APPARATUS
    111.
    发明申请
    SEPARATION METHOD AND APPARATUS 有权
    分离方法和装置

    公开(公告)号：US20110289964A1

    公开(公告)日：2011-12-01

    申请号：US13205196

    申请日：2011-08-08

    申请人： Henry Edward Howard ,  Richard John Jibb

    发明人： Henry Edward Howard ,  Richard John Jibb

    IPC分类号： F25J3/04 ,  F25J3/00

    CPC分类号： F25J3/04787 ,  F25J3/04024 ,  F25J3/0409 ,  F25J3/0423 ,  F25J3/0429 ,  F25J3/04296 ,  F25J3/04303 ,  F25J3/04345 ,  F25J3/04412 ,  F25J3/04781 ,  F25J3/04812 ,  F25J5/002 ,  F25J2210/04 ,  F25J2240/42 ,  F25J2245/40 ,  F25J2290/42 ,  Y10S62/901 ,  Y10S62/903

    摘要： Separation method and apparatus for separating a gaseous mixture, for example, air, in a cryogenic rectification plant in which a compressed stream is divided into subsidiary streams that are extracted from a main heat exchanger of the plant at higher and lower temperatures. The two streams are then combined and expanded in a turboexpander to generate refrigeration for the plant. The flow rates of the two streams are adjusted to control inlet temperature of a turboexpander supplying plant refrigeration and to minimize potential deviation of the turboexpander exhaust from a saturated vapor state. Control of the expansion ratio can advantageously be applied to allow variable liquid production from the rectification plant.

    摘要翻译： 在低温精馏装置中分离气体混合物例如空气的分离方法和装置，其中压缩流被分成在较高和较低温度下从设备的主热交换器中提取的副流。 然后将两股流在涡轮膨胀机中组合并膨胀以产生用于该设备的冷冻。 调节两个流的流速以控制涡轮膨胀机供应设备制冷的入口温度，并使涡轮膨胀机排气从饱和蒸汽状态的潜在偏差降到最小。 膨胀比的控制可以有利地应用于允许来自精馏装置的可变液体生产。

    Separation method and apparatus
    113.
    发明授权
    Separation method and apparatus 有权
    分离方法和装置

    公开(公告)号：US08020408B2

    公开(公告)日：2011-09-20

    申请号：US11634623

    申请日：2006-12-06

    申请人： Henry Edward Howard ,  Richard John Jibb

    发明人： Henry Edward Howard ,  Richard John Jibb

    IPC分类号： F25J3/00

    CPC分类号： F25J3/04787 ,  F25J3/04024 ,  F25J3/0409 ,  F25J3/0423 ,  F25J3/0429 ,  F25J3/04296 ,  F25J3/04303 ,  F25J3/04345 ,  F25J3/04412 ,  F25J3/04781 ,  F25J3/04812 ,  F25J5/002 ,  F25J2210/04 ,  F25J2240/42 ,  F25J2245/40 ,  F25J2290/42 ,  Y10S62/901 ,  Y10S62/903

    摘要： Separation method and apparatus for separating a gaseous mixture, for example, air, in a cryogenic rectification plant in which a compressed stream is divided into subsidiary streams that are extracted from a main heat exchanger of the plant at higher and lower temperatures. The two streams are then combined and expanded in a turboexpander to generate refrigeration for the plant. The flow rates of the two streams are adjusted to control inlet temperature of a turboexpander supplying plant refrigeration and to minimize potential deviation of the turboexpander exhaust from a saturated vapor state. Control of the expansion ratio can advantageously be applied to allow variable liquid production from the rectification plant.

    摘要翻译： 在低温精馏装置中分离气体混合物例如空气的分离方法和装置，其中压缩流被分成在较高和较低温度下从设备的主热交换器中提取的副流。 然后将两股流在涡轮膨胀机中组合并膨胀以产生用于该设备的冷冻。 调节两个流的流速以控制涡轮膨胀机供应设备制冷的入口温度，并使涡轮膨胀机排气从饱和蒸汽状态的潜在偏差降到最小。 膨胀比的控制可以有利地应用于允许来自精馏装置的可变液体生产。

    DISTILLATION METHOD AND APPARATUS
    115.
    发明申请
    DISTILLATION METHOD AND APPARATUS 审中-公开
    蒸馏方法和装置

    公开(公告)号：US20090241595A1

    公开(公告)日：2009-10-01

    申请号：US12056956

    申请日：2008-03-27

    申请人： Murali Chinta ,  Robert Leroy Baker ,  Jeremiah Rauch

    发明人： Murali Chinta ,  Robert Leroy Baker ,  Jeremiah Rauch

    IPC分类号： F25J3/04

    CPC分类号： F25J3/04133 ,  F25J3/04024 ,  F25J3/0409 ,  F25J3/04296 ,  F25J3/04412 ,  F25J3/04781 ,  F25J3/04812 ,  F25J2230/40 ,  F25J2240/10 ,  F25J2245/40

    摘要： A distillation method and apparatus having application to the distillation of air in which liquid production make is varied by varying the pressure ratio across a turboexpander used in generating refrigeration. The pressure ratio is varied by varying the pressure of a compressed stream fed to the turboexpander. This is done by solely compressing such compressed stream by a first booster compressor during a low rate of production of liquid products. During a high rate of production of liquid products, the compressed stream is also compressed within a second booster compressor. The second booster compressor is driven by a variable speed drive to allow a variety of liquid production rates between the low level of liquid production and the high level of liquid production.

    摘要翻译： 通过改变用于产生制冷的涡轮膨胀机的压力比来改变应用于液体生产所产生的空气的蒸馏的蒸馏方法和装置。 通过改变供给到涡轮膨胀机的压缩流的压力来改变压力比。 这是通过在液体产物的低生产率期间由第一增压压缩机单独压缩这种压缩流来完成的。 在液体产品的高生产率期间，压缩流也在第二增压压缩机内被压缩。 第二增压压缩机由变速驱动器驱动，以允许在低液位生产和高水平液体生产之间的各种液体生产速率。

    Process and apparatus for the separation of air by cryogenic distillation
    116.
    发明授权
    Process and apparatus for the separation of air by cryogenic distillation 失效
    通过低温蒸馏分离空气的方法和装置

    公开(公告)号：US06962062B2

    公开(公告)日：2005-11-08

    申请号：US10732673

    申请日：2003-12-10

    申请人： Bao Ha ,  Jean-Renaud Brugerollle

    发明人： Bao Ha ,  Jean-Renaud Brugerollle

    IPC分类号： F25J3/04 ,  F25J3/00

    CPC分类号： F25J3/04175 ,  F25J3/04024 ,  F25J3/04054 ,  F25J3/04084 ,  F25J3/0409 ,  F25J3/04133 ,  F25J3/04278 ,  F25J3/04296 ,  F25J3/04303 ,  F25J3/04309 ,  F25J3/04315 ,  F25J3/04375 ,  F25J3/04381 ,  F25J3/04393 ,  F25J3/04412 ,  F25J2205/04 ,  F25J2230/20 ,  F25J2270/90

    摘要： A method for separating air by cryogenic distillation. A first compressor compresses air to a first pressure, and sends part of that air to a second compressor which compresses that part to a second pressure. Part of the air at the second pressure is cooled in a heat exchanger and sent to a third compressor where part of it is compressed to a third pressure. Part of the air at the third pressure is liquefied and sent a column system. Around half of the total liquefied air sent to the column system will have originally been compressed by the third compressor. Part of the air at the first pressure is cooled in a heat exchanger and part of the cooled air at the first pressure is then expanded to the pressure of the column system. The expanded air is sent to the column system.

    摘要翻译： 一种通过低温蒸馏分离空气的方法。 第一压缩机将空气压缩至第一压力，并将该空气的一部分送到第二压缩机，该第二压缩机将该部分压缩至第二压力。 在第二压力下的一部分空气在热交换器中被冷却并送到第三压缩机，其中一部分被压缩到第三压力。 部分空气在第三个压力下被液化并送出一个柱系统。 送到立柱系统的液化气的大约一半将最初被第三台压缩机压缩。 第一压力的一部分空气在热交换器中冷却，并且在第一压力下的一部分冷却的空气然后膨胀至塔系统的压力。 膨胀的空气被送到塔系统。

    Process and device for the production of a pressurized gaseous product by low-temperature separation of air
    120.
    发明授权
    Process and device for the production of a pressurized gaseous product by low-temperature separation of air 失效
    通过低温分离空气来生产加压气态产品的方法和装置

    公开(公告)号：US06185960B1

    公开(公告)日：2001-02-13

    申请号：US09288226

    申请日：1999-04-08

    申请人： Jürgen Voit

    发明人： Jürgen Voit

    IPC分类号： F25J100

    CPC分类号： F25J3/04957 ,  F25J3/04018 ,  F25J3/04024 ,  F25J3/04084 ,  F25J3/0409 ,  F25J3/04145 ,  F25J3/04296 ,  F25J3/04345 ,  F25J3/04418 ,  F25J3/04448 ,  F25J3/04496 ,  F25J3/04509 ,  F25J3/04781 ,  F25J3/04878 ,  F25J2200/54 ,  F25J2230/24 ,  F25J2230/40 ,  F25J2235/42 ,  F25J2240/42 ,  F25J2290/62 ,  Y10S62/90

    摘要： In a process for the production of a pressurized gaseous product by low-temperature separation of air, which is at times done in a gas operation and at times in a combined operation, whereby in the gas operation and in the combined operation (a) purified charging air is cooled under pressure, partially liquefied, and subjected to rectification to produce gaseous and liquid fractions, (b) extremely cold liquid of at least one of the liquid fractions from the rectification is evaporated under elevated pressure by indirect heat exchange with feed air, heated, and obtained as a pressurized gaseous product, whereby in combined operation, (c) the cold that is required for this purpose is generated in an air-refrigeration cycle, by air being compressed in the refrigeration cycle and work expanded, in which case heat is removed from the air, and the actively depressurized air that is partially in countercurrent is heated again with the charging air that is to be cooled and then repressurized, (d) extremely cold liquid is produced and at least partially stored. During gas operation, the air throughput in the refrigeration cycle is reduced to zero, and extremely cold stored liquid is used to compensate for cold losses that are no longer covered by the refrigeration cycle. In the corresponding apparatus, during gas operation the compressor(s) for the supply of recycle air are switched off in a compressor station for recycle air and throttle air.

    摘要翻译： 在通过低温分离空气生产加压气态产物的过程中，空气有时在气体操作中和有时在组合操作中进行，由此在气体操作和组合操作中（a）纯化的 加压空气在压力下冷却，部分液化，并进行精馏以产生气态和液体馏分，（b）来自精馏的至少一种液体馏分的极冷的液体在高压下通过与进料空气的间接热交换而蒸发 被加热并作为加压气体产物获得，由此在组合操作中，（c）为此目的所需的冷却是在制冷循环中产生的，空气在制冷循环中被压缩并且工作膨胀，其中 从空气中除去外壳的热量，并且将部分逆流的主动减压的空气再次用待冷却的加入空气再次加热，然后再加压， （d）产生极冷的液体并至少部分储存。 在气体操作期间，制冷循环中的空气通过量减少到零，并且使用非常冷的储存液体来补偿不再被制冷循环覆盖的冷损失。 在相应的装置中，在气体运行期间，在用于再循环空气和节流空气的压缩机站中关闭用于供应循环空气的压缩机。