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81.发明授权
公开(公告)号：US5906113A
公开(公告)日：1999-05-25
申请号：US56708
申请日：1998-04-08
CPC分类号： F25J3/04296 , F25J3/04175 , F25J3/0426 , F25J3/04424 , F25J2215/44 , F25J2235/42 , F25J2245/42
摘要： A serial column system for producing relatively large quantities of both high purity nitrogen gas and high purity nitrogen liquid using a first column producing the high purity gas and a second column producing the high purity liquid, with second column top fluid refluxing the first column.
摘要翻译： 使用产生高纯度气体的第一塔产生相对大量的高纯度氮气和高纯度氮液的串联柱系统，以及产生高纯度液体的第二塔，第二塔顶流体回流到第一塔。
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公开(公告)号：US5857357A
公开(公告)日：1999-01-12
申请号：US897008
申请日：1997-07-18
CPC分类号： F25J3/04193 , F25J3/04303 , F25J3/04412 , F25J3/04678 , F25J3/04721 , F25J2200/90 , F25J2290/10 , Y10S62/906 , Y10S62/924
摘要： A system for achieving a low level of nitrogen in a lower pressure column in the feed to the argon column in a cryogenic air separation system by use of two beds of structured packing of about equal height in the lower pressure column, with mixing and redistribution of liquid between them. The packed beds are located between the feed from the argon column top condenser and the point where the argon column feed is withdrawn.
摘要翻译： 一种用于在低温空气分离系统中通过使用两个相等高度的规则填料床在低压塔中进入氩塔的进料中的低压塔中实现低水平氮的系统，混合和重新分配 液体之间。 填充床位于氩塔顶部冷凝器的进料和氩柱进料的抽出点之间。
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公开(公告)号：US5802872A
公开(公告)日：1998-09-08
申请号：US902919
申请日：1997-07-30
CPC分类号： F25J3/044 , F25J3/0409 , F25J3/04206 , F25J3/04218 , F25J3/04296 , F25J3/04303 , F25J3/04412 , F25J2205/24 , Y10S62/909
摘要： A method is provided for separation of air by cryogenic rectification comprising compressing feed air, passing the compressed feed air through a prepurifier wherein the air is substantially cleaned of impurities, thereafter cooling the cleaned air in a cooled regenerator and then introducing it into a cryogenic air separation facility wherein it is separated into nitrogen-rich and oxygen-rich components.
摘要翻译： 提供了一种用于通过低温精馏分离空气的方法，包括压缩进料空气，使压缩的进料空气通过预纯化器，其中空气基本上清除杂质，然后在冷却的再生器中冷却清洁的空气，然后将其引入低温空气 分离设备，其中其被分离成富氮和富氧组分。
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公开(公告)号：US5799505A
公开(公告)日：1998-09-01
申请号：US901350
申请日：1997-07-28
申请人： Dante Patrick Bonaquist , Nancy Rose Cribbin , Joseph Alfred Weber , John Fredric Billingham , Neno Todorov Nenov
发明人： Dante Patrick Bonaquist , Nancy Rose Cribbin , Joseph Alfred Weber , John Fredric Billingham , Neno Todorov Nenov
CPC分类号： F25J1/0232 , F25J1/0015 , F25J1/0017 , F25J1/0037 , F25J1/004 , F25J1/0202 , Y10S62/908
摘要： A system for producing cryogenic liquefied industrial gas, especially useful in conjunction with a non-cryogenic industrial gas production facility, wherein the output of the industrial gas production facility is pressurized, a portion passed to the use point, and another portion is condensed against a turboexpanded stream which is also taken from the pressurized gas.
摘要翻译： 一种用于生产低温液化工业气体的系统，特别适用于非低温工业气体生产设备，其中工业气体生产设备的输出被加压，部分通过使用点，另一部分被冷凝成一个 涡轮膨胀流也是从加压气体中取出的。
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85.发明授权Cryogenic rectification system for producing lower purity oxygen and higher purity oxygen 失效用于生产低纯度氧和较高纯度氧的低温精馏系统
公开(公告)号：US5682766A
公开(公告)日：1997-11-04
申请号：US764431
申请日：1996-12-12
CPC分类号： F25J3/04672 , F25J3/0409 , F25J3/04175 , F25J3/04296 , F25J3/04393 , F25J3/04418 , F25J3/04678 , F25J2200/34 , F25J2200/54 , F25J2200/94 , F25J2205/04 , F25J2215/52 , F25J2215/54
摘要： A cryogenic rectification system having high recovery of both higher purity and lower purity oxygen which employs a side column having a bottom reboiler wherein feed air is partially condensed and the feed air vapor remaining after the partial condensation is turboexpanded prior to rectification.
摘要翻译： 一种具有较高纯度和较低纯度氧的高回收率的低温精馏系统，其使用具有底部再沸器的侧柱，其中进料空气部分冷凝，并且在部分冷凝之后残留的进料空气蒸汽在精馏之前被涡轮膨胀。
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86.发明授权Cryogenic rectification system for producing low purity oxygen and high purity oxygen 失效用于生产低纯氧和高纯氧的低温精馏系统
公开(公告)号：US5669236A
公开(公告)日：1997-09-23
申请号：US691963
申请日：1996-08-05
IPC分类号： F25J3/04
CPC分类号： F25J3/04939 , B01D3/141 , F25J3/04412 , F25J2200/34 , F25J2215/52 , Y10S62/90
摘要： A cryogenic rectification system employing an additional rectifying section in parallel with the lower section of the lower pressure column of a double column for producing product oxygen at both low and high purity.
摘要翻译： 一种低温精馏系统，其采用与双塔低压塔的下段平行的附加精馏段，以产生低纯度和高纯度的产物氧。
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公开(公告)号：US5666824A
公开(公告)日：1997-09-16
申请号：US617591
申请日：1996-03-19
IPC分类号： F25J3/04
CPC分类号： F25J3/04103 , F25J3/0409 , F25J3/04206 , F25J3/04303 , F25J3/04412 , F25J3/04884 , F25J3/04896 , F25J2200/54 , F25J2200/90 , F25J2205/02 , F25J2250/02 , F25J2250/40 , F25J2250/50 , Y10S62/903 , Y10S62/905
摘要： A double column cryogenic rectification system for producing lower purity oxygen wherein a minor portion of the feed air is successively condensed in two vertically oriented stages within the lower pressure column before undergoing rectification.
摘要翻译： 一种用于生产较低纯度氧气的双塔低温精馏系统，其中在进行精馏之前，少部分进料空气在低压塔内的两个垂直取向的级相继冷凝。
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公开(公告)号：US20140044604A1
公开(公告)日：2014-02-13
申请号：US14053177
申请日：2013-10-14
IPC分类号： B01J19/08
CPC分类号： B01J19/087 , B01D53/326 , B01D2256/20 , B01D2257/504 , C25B1/00 , Y02E60/364 , Y02P20/152
摘要： A method and apparatus for producing a carbon monoxide containing product in which cathode and anode sides of an electrically driven oxygen separation device are contacted with carbon dioxide and a reducing agent, respectively. The carbon dioxide is reduced to carbon monoxide through ionization of oxygen and the reducing agent lowers the partial pressure of oxygen at the anode side to partially drive oxygen ion transport within the device through the consumption of the oxygen and to supply heat. The lowering of oxygen partial pressure reduces voltage and therefore, electrical power required to be applied to the device and the heat is supplied to heat the device to an operational temperature and to the reduction of the carbon dioxide occurring at the cathode side. The device can be used as part of an integrated apparatus in which the carbon dioxide is supplied from a waste stream of a process plant.
摘要翻译： 一种含有一氧化碳的产品的制造方法和装置，其中电驱动氧分离装置的阴极和阳极侧分别与二氧化碳和还原剂接触。 通过氧离子将二氧化碳还原成一氧化碳，并且还原剂降低了阳极侧氧的分压，从而通过消耗氧并部分地驱动装置内的氧离子转运。 氧分压的降低降低了电压，因此，需要施加到装置上的电力和热被供给以将装置加热到工作温度并减少在阴极侧发生的二氧化碳。 该装置可以用作集成装置的一部分，其中二氧化碳从处理厂的废物流供应。
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公开(公告)号：US08535415B2
公开(公告)日：2013-09-17
申请号：US13571801
申请日：2012-08-10
IPC分类号： B01D53/047 , C01B3/50
CPC分类号： F25J3/0655 , B01D53/047 , B01D2256/16 , B01D2259/416 , C01B3/506 , C01B3/56 , C01B2203/0465 , C01B2203/0475 , C01B2203/048 , C01B2203/0485 , C01B2203/0495 , F25J3/0219 , F25J3/0233 , F25J3/0238 , F25J3/0252 , F25J3/062 , F25J3/0635 , F25J2200/70 , F25J2205/04 , F25J2205/40 , F25J2205/80 , F25J2210/02 , F25J2210/12 , F25J2245/02
摘要： A process and system for recovering valuable by-products (e.g., hydrogen) from refinery gas streams. For hydrogen-only recovery, the invention comprises a partial condensation step to upgrade the refinery fuel gas to a minimum of 60% hydrogen, which is further purified in a pressure swing adsorption process. When configured to recover hydrogen, methane-rich gas and raw LPG (methane depleted gas containing C2 hydrocarbons and heavier), the invention comprises two partial condensation steps where the feed is cooled in the first step to allow separation of ethane and heavier hydrocarbons, and the resulting vapor is cooled to a lower temperature in a second step for hydrogen recovery.
摘要翻译： 用于从炼油厂气流中回收有价值的副产物（例如氢气）的方法和系统。 对于仅氢回收，本发明包括部分冷凝步骤，以将炼油厂燃料气体升级至至少60％的氢气，其在变压吸附过程中进一步纯化。 当配置回收氢气，富含甲烷的气体和原始LPG（含有C2烃和较重的甲烷贫化气体）时，本发明包括两个部分冷凝步骤，其中进料在第一步骤中冷却以允许乙烷和较重烃分离， 在第二步骤中将所得蒸汽冷却至较低温度以进行氢气回收。
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公开(公告)号：US08262772B2
公开(公告)日：2012-09-11
申请号：US12515181
申请日：2007-12-05
IPC分类号： B01D53/047 , F25J3/00 , C01B3/50
CPC分类号： F25J3/0655 , B01D53/047 , B01D2256/16 , B01D2259/416 , C01B3/506 , C01B3/56 , C01B2203/0465 , C01B2203/0475 , C01B2203/048 , C01B2203/0485 , C01B2203/0495 , F25J3/0219 , F25J3/0233 , F25J3/0238 , F25J3/0252 , F25J3/062 , F25J3/0635 , F25J2200/70 , F25J2205/04 , F25J2205/40 , F25J2205/80 , F25J2210/02 , F25J2210/12 , F25J2245/02
摘要： A process and system for recovering valuable by-products (e.g., hydrogen) from refinery gas streams. For hydrogen-only recovery, the invention comprises a partial condensation step to upgrade the refinery fuel gas to a minimum of 60% hydrogen, which is further purified in a pressure swing adsorption process. When configured to recover hydrogen, methane-rich gas and raw LPG (methane depleted gas containing C2 hydrocarbons and heavier), the invention comprises two partial condensation steps where the feed is cooled in the first step to allow separation of ethane and heavier hydrocarbons, and the resulting vapor is cooled to a lower temperature in a second step for hydrogen recovery.
摘要翻译： 用于从炼油厂气流中回收有价值的副产物（例如氢气）的方法和系统。 对于仅氢回收，本发明包括部分冷凝步骤，以将炼油厂燃料气体升级至至少60％的氢气，其在变压吸附过程中进一步纯化。 当配置回收氢气，富含甲烷的气体和原始LPG（含有C2烃和较重的甲烷贫化气体）时，本发明包括两个部分冷凝步骤，其中进料在第一步骤中冷却以允许乙烷和较重烃分离， 在第二步骤中将所得蒸汽冷却至较低温度以进行氢气回收。
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