专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明授权

US4797141A Method for obtaining CO.sub.2 and N.sub.2 from internal combustion engine or turbine generated gases 失效
标题翻译：从内燃机或涡轮发电气体获得二氧化碳和氮气的方法
公开(公告)号：US4797141A
公开(公告)日：1989-01-10
申请号：US88805
申请日：1987-08-24
申请人： Juan P. Mercader , Pablo R. Villamanan
发明人： Juan P. Mercader , Pablo R. Villamanan
IPC分类号： C01B21/04 , C01B32/50 , F02G5/02 , F25J3/00
CPC分类号： B01D53/75 , B01D53/40 , B01D53/82 , C01B21/0494 , C01B31/20 , F02G5/02 , B01D2253/108 , B01D2256/22 , B01D53/0462 , B01D53/047 , B01D53/0473 , Y02C10/06 , Y02P20/123 , Y02P20/124 , Y02P20/152 , Y02T10/166 , Y10S62/929 , Y10S62/93
摘要： The method consists of recovering heat contained in the combustion gases in a first heat exchanger or boiler, recovering the heat given off by the engine or turbine in the form of steam and/or hot water, leading the previously cooled, in a second heat exchanger, combustion gases to a pressure gas holder, impelling the gases to a washing and cooling column and passing them through CO.sub.2 absorption columns wherein this latter is picked up whereas the remainder of gases, specially N.sub.2, are left free, and conventionally performing the steps for obtaining both gases. For performing all of the obtention procedure, use is made of only the combustion generated energy, thus thoroughly recovering the above gases with a whole benefit of the energy contributed by the hydrocarbons.
摘要翻译：该方法包括回收第一热交换器或锅炉中包含在燃烧气体中的热量，回收由蒸汽和/或热水形式的发动机或涡轮机排出的热量，引导先前冷却的第二热交换器将燃烧气体引导到压力气体保持器，将气体推动到洗涤和冷却塔并将其通过二氧化碳吸收塔，其中后者被吸收，而其余的气体，特别是N2是保持游离的，并且常规地执行以下步骤：获得两种气体。为了执行所有的获取程序，仅使用燃烧产生的能量，从而以碳氢化合物所贡献的能量的全部益处彻底地回收上述气体。

2. 发明授权

US5120338A Method for separating a multi-component feed stream using distillation and controlled freezing zone 失效
标题翻译：使用蒸馏和控制冷冻区分离多组分进料流的方法
公开(公告)号：US5120338A
公开(公告)日：1992-06-09
申请号：US669167
申请日：1991-03-14
申请人： William A. Potts, Jr. , Eugene R. Thomas
发明人： William A. Potts, Jr. , Eugene R. Thomas
IPC分类号： F25J3/02
CPC分类号： F25J3/0209 , F25J3/0233 , F25J3/0266 , F25J2200/02 , F25J2200/74 , F25J2205/20 , F25J2220/66 , F25J2280/40 , Y02C10/12 , Y10S62/927 , Y10S62/929 , Y10S62/93
摘要： The invention relates to a method for separating two primary components of a multi-component feed stream (e.g., methane and nitrogen) in the presence of a third, freezable component (e.g., carbon dioxide) having a relative volatility less than that of either primary component. The inventive process employs both a distillation section and a controlled freezing zone ("CFZ"). The freezable component is allowed to freeze in the CFZ, and the resulting solids are collected at the bottom of the CFZ. The CFZ also produces a vapor overhead product enriched in one of the primary components and a liquid bottom product enriched in the other primary component. The solids of the freezable component are melted and mixed with the CFZ liquid bottom product to form a liquid feed stream for the distillation section which operates like a conventional distillation section, while tolerating significantly high concentrations (i.e., >0.1 mole %) of the freezable component without solids formation, at temperatures well below the freezable component's freezing point.
摘要翻译：本发明涉及一种分离多组分进料流（例如甲烷和氮气）的两种主要组分的方法，该方法在第三种可冷冻组分（例如二氧化碳）存在下，其相对挥发度小于任一种零件。本发明的方法既采用蒸馏段又控制冷冻区（“CFZ”）。允许可冷冻组分在CFZ中冷冻，并将所得固体收集在CFZ的底部。 CFZ还产生富含一种主要组分的蒸气塔顶馏出物和富含另一种主要组分的液体底部产物。将可冷冻组分的固体熔融并与CFZ液体底部产物混合以形成用于蒸馏部分的液体进料流，其运行类似于常规蒸馏部分，同时容许可冷冻的显着高浓度（即> 0.1摩尔％）组分无固体形成，温度远低于可冷冻组分的凝固点。

3. 发明授权

US2966036A Method and apparatus for processing products of combustion 失效
标题翻译：用于加工燃烧产物的方法和装置
公开(公告)号：US2966036A
公开(公告)日：1960-12-27
申请号：US79435159
申请日：1959-02-19
申请人： DANIEL STOWENS
发明人： DANIEL STOWENS
IPC分类号： F01N3/08
CPC分类号： F01N3/08 , F01N2240/22 , F01N2240/26 , Y10S55/30 , Y10S62/93

4. 发明授权

US4149864A Separation of carbon dioxide and other acid gas components from hydrocarbon feeds 失效
标题翻译：从碳氢化合物进料中分离二氧化碳和其他酸性气体组分
公开(公告)号：US4149864A
公开(公告)日：1979-04-17
申请号：US833937
申请日：1977-09-16
申请人： James M. Eakman , Harry A. Marshall
发明人： James M. Eakman , Harry A. Marshall
IPC分类号： B01D53/00 , F25J3/02
CPC分类号： B01D53/00 , C01B3/506 , F25J3/0209 , F25J3/0219 , F25J3/0223 , F25J3/0233 , F25J3/0252 , F25J3/0266 , F25J3/0271 , C01B2203/0475 , F25J2200/02 , F25J2200/74 , F25J2210/12 , Y02C10/12 , Y02P20/152 , Y10S62/929 , Y10S62/93
摘要： A process for the separation of carbon dioxide and, optionally, other acid gas components in a distillation column, operated at high pressure and low temperature, from a gaseous mixture comprising one or more hydrocarbons, including particularly methane, and hydrogen. In its preferred aspects, the feed is predominantly methane, suitably from about 30 to about 85 mole percent and preferably from about 50 to about 80 mole percent methane. The concentration of hydrogen in the gaseous mixture will be sufficient to provide from about 6 to about 34 mole percent, preferably from about 15 to about 25 mole percent hydrogen in the rectification portion of the distillation column. The separation can be effected in a single column usually having from about 20 to about 30 theoretical distillation stages and the feed can be one constituted ab initio within the desired ranges of composition, or modified by addition of components just prior to or at the time of distillation.
摘要翻译：从包括一种或多种烃，特别是甲烷和氢的气体混合物中分离在高压和低温下运行的蒸馏塔中的二氧化碳和任选的其它酸性气体组分的方法。在其优选的方面，进料主要是甲烷，合适地为约30至约85摩尔％，优选约50至约80摩尔％的甲烷。气态混合物中的氢气浓度足以在蒸馏塔的精馏部分提供约6至约34摩尔％，优选约15至约25摩尔％的氢气。分离可以在通常具有约20至约30个理论蒸馏阶段的单个塔中进行，并且进料可以是在所需组合物范围内从头开始，或者通过在刚刚之前或之后添加组分进行修饰蒸馏。

5. 发明授权

US3718006A Process for selective absorption 失效
标题翻译：选择性吸收方法
公开(公告)号：US3718006A
公开(公告)日：1973-02-27
申请号：US3718006D
申请日：1969-12-09
申请人： LINDE AG
发明人： RANKE G , JUNGFER H
IPC分类号： B01D53/18 , F25J3/02 , F25J3/08 , B01D53/14 , F25J5/00
CPC分类号： B01D53/18 , B01D53/1462 , B01D53/1468 , B01D53/1475 , Y02C10/06 , Y10S62/929 , Y10S62/93
摘要： A process for the removal of at least one component from a gaseous mixture by selective absorption in a solvent, said component having an exothermic heat of solution in said solvent, said process comprising the steps of: A. PASSING SAID GASEOUS MIXTURE INTO THE BOTTOM ZONE OF AN ABSORPTION COLUMN HAVING TOP, MIDDLE AND BOTTOM ZONES; B. PASSING SAID SOLVENT INTO THE TOP ZONE OF SAID ABSORPTION COLUMN; C. WITHDRAWING PARTIALLY ABSORBED GASEOUS MIXTURE FROM THE MIDDLE ZONE OF SAID COLUMN; D. COOLING SAID PARTIALLY ABSORBED GASEOUS MIXTURE; E. RECYCLING RESULTANT COOLED MIXTURE TO SAID ABSORPTION COLUMN; AND F. FURTHER CONTACTING RESULTANT RECYCLED COOLED GASEOUS MIXTURE WITH SAID SOLVENT TO COMPLETE SAID ABSORPTION.
摘要翻译：一种通过在溶剂中选择性吸收从气态混合物中除去至少一种组分的方法，所述组分在所述溶剂中具有溶液的放热热，所述方法包括以下步骤：

6. 发明授权

US5233837A Process and apparatus for producing liquid carbon dioxide 失效
标题翻译：生产液态二氧化碳的方法和设备
公开(公告)号：US5233837A
公开(公告)日：1993-08-10
申请号：US940281
申请日：1992-09-03
申请人： Richard A. Callahan
发明人： Richard A. Callahan
IPC分类号： F01K17/04 , B01D53/22 , C01B21/04 , C01B32/50 , F25J3/02 , F25J3/06
CPC分类号： F25J3/067 , B01D53/229 , C01B21/045 , C01B31/20 , F25J3/066 , C01B2210/0051 , F25J2205/40 , F25J2205/80 , F25J2210/04 , F25J2210/42 , F25J2210/70 , F25J2215/04 , F25J2220/44 , F25J2220/82 , F25J2230/30 , F25J2240/12 , F25J2245/90 , F25J2270/14 , Y02C10/12 , Y02E20/14 , Y02P20/129 , Y02P20/13 , Y02P20/152 , Y10S62/93
摘要： A process for producing liquid carbon dioxide. A process stream which comprises carbon dioxide, balance substantially nitrogen and water, is cooled so that a minor amount of the water is condensed out. The process stream is compressed so that substantially all of the water but trace amounts is condensed out. Next, the process stream is cleaned to remove the trace amounts of water, any long-chain hydrocarbons present and any particulates present. The process stream is then separated into a nitrogen-rich gaseous stream and a carbon dioxide-rich gaseous stream. The carbon dioxide-rich gaseous stream is then compressed and the nitrogen-rich gaseous stream is expanded to produce an expanded nitrogen-rich gaseous stream. The energy of the expanding is used to compress the carbon dioxide-rich gaseous stream. The compressed carbon dioxide-rich gaseous stream is cooled to liquefy the carbon dioxide in the stream and reduce the temperature of the gaseous nitrogen in the stream. The liquefied carbon dioxide is withdrawn as product. The liquefying of the carbon dioxide-rich gaseous stream is by using the expanded nitrogen-rich gaseous stream. After the liquefying, the nitrogen-rich gaseous stream is used to perform at least part of the first cooling. In a preferred form, the process stream results from combusting a mixture of fuel and oxygen in a heat engine to drive an electrical generator with the product of the heat engine to produce electricity and also yielding the process stream. Apparatus for the production of liquid carbon dioxide which includes devices to perform each of the process steps.
摘要翻译：一种生产液态二氧化碳的方法。包含二氧化碳，基本上平衡氮和水的工艺流被冷却，使得少量的水冷凝出来。将工艺物流压缩，使得基本上所有的水，但痕量都被冷凝出来。接下来，清洁工艺流以除去痕量的水，存在的任何长链烃和存在的任何颗粒。然后将工艺流分离成富氮气流和富含二氧化碳的气流。然后将富含二氧化碳的气流压缩，并使富氮气流膨胀以产生膨胀的富氮气流。膨胀的能量用于压缩富含二氧化碳的气流。将压缩的富含二氧化碳的气流冷却以使物流中的二氧化碳液化并降低气流中的气态氮的温度。液化二氧化碳作为产品被取出。富含二氧化碳的气流的液化是通过使用膨胀的富氮气流。液化后，使用富氮气流进行至少部分第一次冷却。在优选的形式中，工艺流是由于在发动机中燃烧燃料和氧气的混合物而产生的，以利用热机的产品来驱动发电机产生电力并产生工艺流。用于生产液体二氧化碳的装置，其包括用于执行每个工艺步骤的装置。

7. 发明授权

US4762543A Carbon dioxide recovery 失效
标题翻译：二氧化碳回收
公开(公告)号：US4762543A
公开(公告)日：1988-08-09
申请号：US27761
申请日：1987-03-19
申请人： Leroy A. Pantermuehl , Thomas E. Krisa
发明人： Leroy A. Pantermuehl , Thomas E. Krisa
IPC分类号： C01B32/50 , E21B43/16 , E21B43/40 , F25J3/02 , F25J3/08
CPC分类号： F25J3/0233 , C01B31/20 , E21B43/164 , E21B43/40 , F25J3/0209 , F25J3/0266 , F25J2200/02 , F25J2200/04 , F25J2200/74 , F25J2205/04 , F25J2215/04 , F25J2220/82 , F25J2230/30 , F25J2235/80 , F25J2260/80 , F25J2270/90 , Y02C10/12 , Y02P20/152 , Y02P90/70 , Y10S62/929 , Y10S62/93
摘要： A novel gas processing method is disclosed which is useful in separating and recovering carbon dioxide from gas streams having a high carbon dioxide content (e.g., 85-95 mol percent) and a low hydrocarbon/nitrogen content. The method is particularly useful in processing gas streams produced during carbon dioxide flooding operations for enhanced oil recovery.
摘要翻译：公开了一种新型的气体处理方法，其可用于从具有高二氧化碳含量（例如85-95摩尔％）和低烃/氮含量的气流中分离和回收二氧化碳。该方法特别可用于处理在二氧化碳驱油操作期间产生的用于提高采油量的气流。

8. 发明授权

US5927103A Carbon dioxide production system with integral vent gas condenser 失效
标题翻译：二氧化碳生产系统采用集成排气冷凝器
公开(公告)号：US5927103A
公开(公告)日：1999-07-27
申请号：US98431
申请日：1998-06-17
申请人： Henry Edward Howard
发明人： Henry Edward Howard
IPC分类号： B01D53/00 , C01B32/50 , F25J3/02 , F25J3/08 , F25J3/00
CPC分类号： F25J3/0266 , B01D53/002 , C01B31/20 , F25J3/08 , F25J2200/02 , F25J2200/70 , F25J2205/02 , F25J2210/04 , F25J2220/82 , F25J2230/04 , F25J2230/30 , F25J2245/02 , F25J2270/02 , F25J2270/90 , Y02C10/12 , Y02P20/152 , Y10S62/928 , Y10S62/93
摘要： A system for producing carbon dioxide, particularly from a feed which contains significant levels of light contaminants, wherein light overhead from a distillation column is partially condensed against heat exchange fluid containing both carbon dioxide and light contaminants and the resulting heat exchange fluid passed into the feed for the distillation column.
摘要翻译：一种用于生产二氧化碳的系统，特别是来自含有显着水平的轻质污染物的进料的系统，其中来自蒸馏塔的轻质塔顶部分冷凝，所述热交换流体包含二氧化碳和轻污染物，所得到的热交换流体进入进料用于蒸馏塔。

9. 发明授权

US2970451A Absorption-desorption in absorber liquid 失效
标题翻译：吸收液中吸收 - 解吸
公开(公告)号：US2970451A
公开(公告)日：1961-02-07
申请号：US71319058
申请日：1958-02-04
申请人： HYDROCARBON RESEARCH INC
发明人： EHRLICH STANLEY W , SZE MORGAN C
IPC分类号： B01D53/14
CPC分类号： B01D53/1475 , Y02C10/06 , Y10S62/929 , Y10S62/93

10. 发明授权

US2143283A Process for production of solidified carbon dioxide and the recovery of nitrogen 失效
标题翻译：生产固化二氧化碳和回收氮气的方法
公开(公告)号：US2143283A
公开(公告)日：1939-01-10
申请号：US5251935
申请日：1935-12-02
申请人： SCHMIDT FRED A
发明人： SCHMIDT FRED A
IPC分类号： C01B32/50 , C01B32/55
CPC分类号： C01B32/55 , C01B32/50 , Y10S62/93

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式