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1. 发明授权

US5749246A Method and device for obtaining oxygen and nitrogen at superatmospheric pressure 失效
标题翻译：用于在超大气压下获得氧气和氮气的方法和装置
公开(公告)号：US5749246A
公开(公告)日：1998-05-12
申请号：US756012
申请日：1996-11-25
申请人： Dietrich Rottmann
发明人： Dietrich Rottmann
IPC分类号： F25J3/04
CPC分类号： F25J3/04915 , F25J3/0409 , F25J3/04103 , F25J3/04212 , F25J3/04321 , F25J3/04363 , F25J3/04424 , F25J3/04678 , F25J3/04878 , F25J2235/50
摘要： The method and the apparatus are used to obtain oxygen and nitrogen at superatmospheric pressure by low-temperature separation of air in a rectification column system. Compressed and purified feed air (1, 3) is introduced into a pressure column (4). Liquids (5, 8) from the lower region and, respectively, from the upper or middle region of the pressure column (4) are fed into the low-pressure column (7). A third liquid fraction (17) from the lower region of the low-pressure column (7) is evaporated in indirect heat exchange (12) with condensing vapour (11) from the upper region of the pressure column (4), at least a portion of the vapour (22, 24, 26, 27) obtained in the process being introduced into the low-pressure column (7). Condensate (13) is fed into the pressure column (4); A pressurized nitrogen fraction (10, 14, 15) is extracted as product from the upper region of the pressure column (4). The pressure of the third liquid fraction (17) from the lower region of the low-pressure column (17) is increased upstream of the indirect heat exchange (12); that portion (24) of the vapor which is obtained during the indirect heat exchange and led back into the low-pressure column is expanded (25) before being introduced (27) into the low-pressure column (7).
摘要翻译：该方法和装置用于通过精馏塔系统中的空气的低温分离而在超大气压下获得氧和氮。将压缩和净化的进料空气（1,3）引入压力塔（4）中。来自下部区域和分别来自压力塔（4）的上部或中部区域的液体（5,8）被供给到低压塔（7）中。来自低压塔（7）的下部区域的第三液体馏分（17）在与压力塔（4）的上部区域的冷凝蒸气（11）的间接热交换（12）中蒸发，至少在该方法中获得的部分蒸汽（22,24,26,27）被引入低压塔（7）中。冷凝物（13）进料到压力塔（4）中; 从压力塔（4）的上部区域提取加压氮气馏分（10,14,15）作为产物。来自低压塔（17）的下部区域的第三液体馏分（17）的压力在间接热交换（12）的上游增加; 在间接热交换期间获得并引导回低压塔的蒸汽的部分（24）在引入（27）之前被膨胀（25）到低压塔（7）中。

2. 发明授权

US5209070A Process and arrangement for the distillation of air in the production of gaseous oxygen under variable operating conditions 失效
标题翻译：在可变操作条件下生产气体氧气中空气的蒸发过程和布置
公开(公告)号：US5209070A
公开(公告)日：1993-05-11
申请号：US801731
申请日：1991-12-03
申请人： Bernard Darredeau
发明人： Bernard Darredeau
IPC分类号： F25J3/04
CPC分类号： F25J3/04303 , F25J3/04363 , F25J3/04412 , F25J3/04509 , F25J3/04678 , F25J2235/42 , F25J2235/50 , Y10S62/913 , Y10S62/939
摘要： This process is of the alternating type. When the demand of oxygen is lower than the mean value, additional liquid oxygen is produced by introducing compressed oxygen, in gaseous form, in the heat exchange line of the arrangement, the flow of liquid nitrogen injected into the double column being reduced in a corresponding manner. It is thus possible to increase the average yield of the arrangement when extracting argon.
摘要翻译：这个过程是交替的。当氧气的需求低于平均值时，通过在该装置的热交换管线中引入气态形式的压缩氧来产生附加的液氧，注入到双塔中的液氮的流动被减少为相应的方式。因此，当提取氩时，可以提高排列的平均产量。

3. 发明授权

US3363426A Gas separation with particular reference to air separation 失效
标题翻译：气体分离，特别是空气分离
公开(公告)号：US3363426A
公开(公告)日：1968-01-16
申请号：US40622764
申请日：1964-10-26
申请人： ROMAN STOKLOSINSKI
发明人： ROMAN STOKLOSINSKI
IPC分类号： F25J3/04
CPC分类号： F25J3/04363 , F25J3/04066 , F25J3/04357 , F25J3/044 , F25J3/04624 , F25J2200/02 , F25J2200/50 , F25J2200/74 , F25J2205/02 , F25J2245/02

4. 发明授权

US5363657A Single column process and apparatus for producing oxygen at above-atmospheric pressure 失效
标题翻译：用于在高于大气压下生产氧气的单柱方法和装置
公开(公告)号：US5363657A
公开(公告)日：1994-11-15
申请号：US60144
申请日：1993-05-13
申请人： Joseph P. Naumovitz
发明人： Joseph P. Naumovitz
IPC分类号： F25J3/04 , F25J3/02
CPC分类号： F25J3/044 , F25J3/04066 , F25J3/0423 , F25J3/04309 , F25J3/04363 , F25J2200/74
摘要： A process and apparatus for separating air in which a refrigerant stream produced at the top of a single column is expanded with the performance of work. Such expansion can be carried out in an expansion machine coupled to a recycle compressor by an energy dissipative brake. An oxygen stream is removed from a bottom region of the column and a compressor compresses an oxygen stream to column pressure which is at an above atmospheric delivery pressure. After compression, the oxygen stream is divided into two partial streams. One of the two partial streams is fed back into a bottom region of the column as a vapor to provide boil up while the other of the two partial streams is taken as a product which having been derrived from the compressed stream is therefore at the above-atmospheric delivery pressure. The refrigerant stream is heat exchanged countercurrently with incoming air to be separated in order to add refrigeration.
摘要翻译：一种用于分离空气的方法和装置，其中在单柱顶部产生的制冷剂流随着工作的进行而膨胀。这种膨胀可以在通过能量耗散制动器连接到再循环压缩机的膨胀机中进行。从柱的底部区域除去氧气流，并且压缩机将氧气流压缩至高于大气输送压力的塔压力。压缩后，将氧气流分成两部分流。两个部分流中的一个作为蒸汽被反馈到塔的底部区域以提供沸腾，而两个部分流中的另一个被认为是从压缩流排出的产物因此处于上述状态，大气输送压力。制冷剂流与要分离的进入空气逆流热交换，以增加制冷。

5. 发明授权

US4574006A Process to produce a krypton-xenon concentrate from a liquid feed 失效
标题翻译：从液体进料生产氪 - 氙浓缩物的方法
公开(公告)号：US4574006A
公开(公告)日：1986-03-04
申请号：US641553
申请日：1984-08-16
申请人： Harry Cheung
发明人： Harry Cheung
IPC分类号： F25J3/04
CPC分类号： F25J3/04412 , F25J3/04363 , F25J3/04745 , F25J3/04963 , F25J2200/34 , F25J2200/94 , F25J2235/50 , F25J2290/62 , Y10S62/925
摘要： A process which produces a krypton-xenon concentrate from a liquid feed while also producing a liquid product substantially free of rare gases. The process employs an integral heat pump circuit to carry out the separation in an energy-efficient manner.
摘要翻译：从液体进料产生氪 - 氙精矿的方法，同时产生基本上不含稀有气体的液体产物。该方法采用一体式热泵电路，以高能效的方式进行分离。

6. 发明授权

US3779028A Improved krypton xenon recovery method 失效
标题翻译：改进的KRYPTON XENON恢复方法
公开(公告)号：US3779028A
公开(公告)日：1973-12-18
申请号：US3779028D
申请日：1971-10-08
申请人： BRITISH OXYGEN CO LTD
发明人： SCHUFTAN P , DAVIS G , ARMOND J , LEADER J
IPC分类号： F25J3/04 , F25J3/02
CPC分类号： F25J3/04224 , F25J3/04303 , F25J3/04363 , F25J3/04412 , F25J3/04745 , F25J2200/34 , F25J2205/60 , F25J2220/52 , F25J2235/50 , Y10S62/925
摘要： Krypton and xenon are recovered from the oxygen produced in the reboiler of an air separation unit by passing the oxygen into a two-section rectification column having at least one reboiler and in which the reflux ratio is selected to give a primary krypton/xenon concentrate of low methane content and containing at least 10 percent krypton.
摘要翻译：将氪和氙从空气分离单元的再沸器中产生的氧气中回收，通过将氧气通入至少一个再沸器的两段式精馏塔中，其中回流比被选择得到主要的氪/氙浓缩物甲烷含量低，含有至少10％的氪。

7. 发明授权

US3208231A Rectification of liquid mixtures boiling at low temperatures 失效
标题翻译：在低温下沸腾的液体混合物的整流
公开(公告)号：US3208231A
公开(公告)日：1965-09-28
申请号：US16311961
申请日：1961-12-29
申请人： LINDE EISMASCH AG
发明人： RUDOLF BECKER
IPC分类号： F25J3/02 , F25J3/04
CPC分类号： F25J3/0238 , F25J3/0219 , F25J3/0252 , F25J3/04351 , F25J3/04363 , F25J3/04454 , F25J3/04872 , F25J2200/08 , F25J2200/40 , F25J2200/50 , F25J2200/54 , F25J2210/12 , F25J2215/62 , F25J2250/20 , F25J2290/40

8. 发明授权

US09458762B2 Method and device for generating electrical energy 有权
标题翻译：用于产生电能的方法和装置
公开(公告)号：US09458762B2
公开(公告)日：2016-10-04
申请号：US13856115
申请日：2013-04-03
申请人： Linde Aktiengesellschaft
发明人： Dimitri Goloubev
IPC分类号： F02C3/00 , F25J3/04
CPC分类号： F02C3/00 , F25J3/04018 , F25J3/0406 , F25J3/04181 , F25J3/04224 , F25J3/04254 , F25J3/04303 , F25J3/04309 , F25J3/04363 , F25J3/04393 , F25J3/04496 , F25J3/04509 , F25J3/04533 , F25J3/04545 , F25J3/04581 , F25J3/04618 , F25J3/04836 , F25J2210/06 , F25J2210/50 , F25J2230/04 , F25J2230/06 , F25J2240/70 , F25J2245/50 , Y02E20/16
摘要： The method and the apparatus described are used for generating electrical energy in a combined system comprising a power plant and a low-temperature air separation unit. A feed air stream is compressed in a main air compressor, cooled, and introduced into a distillation column system having a high-pressure column and a low-pressure column. A first oxygen-enriched stream from the distillation column system is introduced into the power plant. In a first operating mode, cryogenic liquid from the distillation column system is introduced into a liquid tank and is stored there at least in part. In a second operating mode, stored cryogenic liquid is removed from the liquid tank and introduced into the distillation column system. A second process fluid from the distillation column system is heated and then actively depressurized in a hot expansion turbine. In addition, in the second operating mode, a nitrogen-enriched product stream from the high-pressure column is also heated to a high temperature and then depressurized in the hot expansion turbine.
摘要翻译：所述的方法和装置用于在包括发电厂和低温空气分离单元的组合系统中产生电能。原料空气流在主空气压缩机中被压缩，冷却，并引入具有高压塔和低压塔的蒸馏塔系统中。将来自蒸馏塔系统的第一富氧物流引入发电厂。在第一操作模式中，来自蒸馏塔系统的低温液体被引入到液体罐中并且至少部分储存在其中。在第二操作模式中，储存的低温液体从液体罐中移出并被引入蒸馏塔系统。来自蒸馏塔系统的第二工艺流体被加热，然后在热膨胀涡轮机中主动减压。此外，在第二操作模式中，来自高压塔的富氮产物流也被加热到高温，然后在热膨胀涡轮中减压。

9. 发明授权

US06327873B1 Cryogenic rectification system for producing ultra high purity oxygen 有权
标题翻译：用于生产超高纯氧的低温精馏系统
公开(公告)号：US06327873B1
公开(公告)日：2001-12-11
申请号：US09593746
申请日：2000-06-14
申请人： James Robert Dray , Scot Eric Jaynes
发明人： James Robert Dray , Scot Eric Jaynes
IPC分类号： F25J100
CPC分类号： F25J3/08 , F25J3/04363 , F25J3/04715 , F25J3/04745 , F25J2200/04 , F25J2200/34 , F25J2210/50 , F25J2215/56 , F25J2220/52 , F25J2250/50 , F25J2270/50 , Y10S62/925
摘要： A cryogenic rectification system comprising an upstream krypton/xenon knockout column and a downstream oxygen upgrader column wherein the knockout column processes a crude feed for removal of heavy components including hydrocarbons and the upgrader column produces ultra high purity oxygen.
摘要翻译：一种低温精馏系统，其包括上游氪/氙敲除柱和下游氧气升级塔，其中所述敲除塔处理粗制原料以除去包括烃的重组分，并且所述升级塔产生超高纯度氧。

10. 发明授权

US5806340A High purity nitrogen generator unit and method 失效
标题翻译：高纯氮发生器单元及方法
公开(公告)号：US5806340A
公开(公告)日：1998-09-15
申请号：US856003
申请日：1997-05-14
申请人： Shinji Tomita
发明人： Shinji Tomita
IPC分类号： F25J3/04
CPC分类号： F25J3/04333 , F25J3/04048 , F25J3/04066 , F25J3/04084 , F25J3/04103 , F25J3/04206 , F25J3/04321 , F25J3/04363 , F25J3/0443 , F25J2200/94 , F25J2205/02 , F25J2210/04 , F25J2215/44 , F25J2220/42 , F25J2230/52 , F25J2245/02 , F25J2250/02 , F25J2250/20 , F25J2250/30 , F25J2250/40 , F25J2250/42 , F25J2250/50
摘要： A high purity nitrogen generator unit which is excellent in the energy efficiency and the recovery of high purity nitrogen gas, is provided. In a rectification column 1, feed air is separated to oxygen-rich liquid air and nitrogen gas. The oxygen-rich liquid air in its bottom is reduced in pressure by a first expansion valve 21 and sent to a composition regulation column 3. The nitrogen gas in its top is condensed in a nitrogen condenser 2, the resulting liquid nitrogen is returned as a reflux liquid to the rectification column 1 and non-condensed gas is released. After oxygen-rich waste gas in the lower part of the composition regulation column 3 is reduced in pressure by an expansion turbine 6, it is released by way of a first heat exchanger 4. Mixed gas in the top of the composition regulation column 3 is introduced for re-circulation into a first compressor 5. Another portion of the mixed gas is returned to the composition regulation column 3 by way of a second compressor 7, second heat exchanger 8 and second expansion valve 22. The second compressor 7 is driven by means of the expansion turbine 6. High purity liquid nitrogen taken out of the vicinity of the top of the rectification column 1 is evaporated for recovery in the second heat exchanger 8.
摘要翻译：提供了能量效率优异和高纯度氮气回收的高纯度氮气发生器单元。在精馏塔1中，将进料空气分离成富氧液体空气和氮气。其底部的富氧液体空气通过第一膨胀阀21减压，并送到组成调节塔3.其顶部的氮气在氮冷凝器2中冷凝，得到的液氮作为回流液到精馏塔1，非冷凝气体被释放。在组成调节塔3的下部的富氧废气通过膨胀涡轮6减压后，通过第一热交换器4释放。组成调节塔3顶部的混合气体为引入再循环到第一压缩机5中。另一部分混合气体通过第二压缩机7，第二热交换器8和第二膨胀阀22返回到组成调节塔3中。第二压缩机7由膨胀涡轮机6的装置。从精馏塔1顶部附近取出的高纯度液氮在第二热交换器8中蒸发回收。

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