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公开(公告)号:US20080308769A1
公开(公告)日:2008-12-18
申请号:US11916688
申请日:2006-05-22
CPC分类号: C01B3/56 , B01D53/04 , B01D53/047 , B01D53/261 , B01D2256/16 , B01D2257/504 , B01D2257/80 , B01D2259/40001 , B01D2259/40052 , B01D2259/414 , C01B3/506 , C01B3/52 , C01B32/40 , C01B2203/0205 , C01B2203/0415 , C01B2203/043 , C01B2203/046 , C01B2203/047 , C01B2203/0475 , F25J3/0223 , F25J3/0233 , F25J3/0252 , F25J3/0261 , F25J2205/40 , F25J2205/60 , F25J2205/66 , F25J2215/02 , F25J2245/02 , Y02C10/08 , Y02P20/133 , Y02P20/152
摘要: The invention relates to a method for simultaneously producing hydrogen and carbon monoxide consisting in generating a synthesis gas and in processing it by decarbonising and removing water and remaining carbon dioxide by passing said gas through a bed of adsorbents, in separating remaining components by forming at least one H 2 -rich flow, a CO flow containing at least one type of impurity selected from nitrogen and argon, a methane-rich purge gas flow and a flash gas flow. The inventive method also consists in regenerating the bed of adsorbents by passing a regeneration gas comprising at least one non-zero proportion of the formed H 2 flow and in recycling at least the purge and flash gases for feeding the synthesis gas generation stage.
摘要翻译: 本发明涉及一种同时生产氢气和一氧化碳的方法,该方法同时产生产生合成气并在通过使所述气体通过吸附剂床脱碳和除去水和剩余二氧化碳进行处理,通过形成至少 一个富H 2 H 2流,含有选自氮和氩的至少一种类型的杂质的CO流,富甲烷吹扫气流和闪蒸气流。 本发明的方法还包括通过使包含至少一个非零比例的形成的H 2 O 2流的再生气体再生,并在至少再循环至少吹扫气体和闪蒸气体之后再生吸附剂床, 合成气生成阶段。
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公开(公告)号:US07731923B2
公开(公告)日:2010-06-08
申请号:US11916688
申请日:2006-05-22
CPC分类号: C01B3/56 , B01D53/04 , B01D53/047 , B01D53/261 , B01D2256/16 , B01D2257/504 , B01D2257/80 , B01D2259/40001 , B01D2259/40052 , B01D2259/414 , C01B3/506 , C01B3/52 , C01B32/40 , C01B2203/0205 , C01B2203/0415 , C01B2203/043 , C01B2203/046 , C01B2203/047 , C01B2203/0475 , F25J3/0223 , F25J3/0233 , F25J3/0252 , F25J3/0261 , F25J2205/40 , F25J2205/60 , F25J2205/66 , F25J2215/02 , F25J2245/02 , Y02C10/08 , Y02P20/133 , Y02P20/152
摘要: The invention relates to a method for simultaneously producing hydrogen and carbon monoxide consisting in generating a synthesis gas and in processing it by decarbonising and removing water and remaining carbon dioxide by passing said gas through a bed of adsorbents, in separating remaining components by forming at least one H2 rich flow, a CO flow containing at least one type of impurity selected from nitrogen and argon, a methane-rich purge gas flow and a flash gas flow. The inventive method also consists in regenerating the bed of adsorbents by passing a regeneration gas comprising at least one non-zero proportion of the formed H2 flow and in recycling at least the purge and flash gases for feeding the synthesis gas generation stage.
摘要翻译: 本发明涉及一种同时生产氢气和一氧化碳的方法,该方法同时产生产生合成气并在通过使所述气体通过吸附剂床脱碳和除去水和剩余二氧化碳进行处理,通过形成至少 一个富H2流,含有选自氮和氩的至少一种类型的杂质的CO流,富甲烷吹扫气流和闪蒸气流。 本发明的方法还包括通过使包含至少一个非零比例形成的H 2流的再生气体再生至少吸收净化气体和闪蒸气体来再生吸附剂床,以供给合成气产生阶段。
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公开(公告)号:US20120292574A1
公开(公告)日:2012-11-22
申请号:US13169270
申请日:2011-06-27
申请人: Paul Terrien , Trapti Chaubey , Purushottam V. Shanbhag , Bhadra S. Grover , Dennis A. Vauk , Arthur Darde , Pascal Marty
发明人: Paul Terrien , Trapti Chaubey , Purushottam V. Shanbhag , Bhadra S. Grover , Dennis A. Vauk , Arthur Darde , Pascal Marty
IPC分类号: C01B3/32
摘要: This present invention provides a method to more efficiently recover hydrogen and carbon dioxide, preferably at least 50%, even more preferably at least 75%, and most preferably at least 90% of the carbon dioxide. The present invention further provides the design for capture of at least 80%, carbon dioxide from syngas that allows for the simultaneous production of medium to high amounts of hydrogen in the syngas as a part of the production of hydrogen in a hydrogen generation plant. By using the process of the present invention, especially in terms of a hydrogen generation plant, it is possible to increase recovery of hydrogen and capture of the carbon dioxide in the syngas stream by balancing the recycle of the hydrogen rich permeate from the hydrogen membrane separation units to the process unit and/or the water gas shift as capacity allows when a carbon dioxide separation unit, a carbon dioxide membrane separation unit and two hydrogen membrane separation units are utilized.
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公开(公告)号:US20120291485A1
公开(公告)日:2012-11-22
申请号:US13169258
申请日:2011-06-27
申请人: Paul Terrien , Trapti Chaubey , Purushottam V. Shanbhag , Bhadra S. Grover , Dennis A. Vauk , Arthur Darde , Pascal Marty
发明人: Paul Terrien , Trapti Chaubey , Purushottam V. Shanbhag , Bhadra S. Grover , Dennis A. Vauk , Arthur Darde , Pascal Marty
IPC分类号: F25J3/08
摘要: This present invention provides a method to more efficiently recover hydrogen and carbon dioxide, preferably at least 50%, even more preferably at least 75%, and most preferably at least 90% of the carbon dioxide. The present invention further provides the design for capture of at least 80%, carbon dioxide from syngas that allows for the simultaneous production of medium to high amounts of hydrogen in the syngas as a part of the production of hydrogen in a hydrogen generation plant. By using the process of the present invention, especially in terms of a hydrogen generation plant, it is possible to increase recovery of hydrogen and capture of the carbon dioxide in the syngas stream by balancing the recycle of the hydrogen rich permeate from the hydrogen membrane separation units to the process unit and/or the water gas shift as capacity allows when a carbon dioxide separation unit, a carbon dioxide membrane separation unit and two hydrogen membrane separation units are utilized.
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公开(公告)号:US20120291484A1
公开(公告)日:2012-11-22
申请号:US13169241
申请日:2011-06-27
申请人: Paul Terrien , Trapti Chaubey , Purushottam V. Shanbhag , Bhadra S. Grover , Dennis A. Vauk , Arthur Darde , Pascal Marty
发明人: Paul Terrien , Trapti Chaubey , Purushottam V. Shanbhag , Bhadra S. Grover , Dennis A. Vauk , Arthur Darde , Pascal Marty
IPC分类号: F25J3/08
摘要: This present invention provides a method to more efficiently recover hydrogen and carbon dioxide, preferably at least 50%, even more preferably at least 75%, and most preferably at least 90% of the carbon dioxide. The present invention further provides the design for capture of at least 80%, carbon dioxide from syngas that allows for the simultaneous production of medium to high amounts of hydrogen in the syngas as a part of the production of hydrogen in a hydrogen generation plant. By using the process of the present invention, especially in terms of a hydrogen generation plant, it is possible to increase recovery of hydrogen and capture of the carbon dioxide in the syngas stream by balancing the recycle of the hydrogen rich permeate from the hydrogen membrane separation units to the process unit and/or the water gas shift as capacity allows when a carbon dioxide separation unit, a carbon dioxide membrane separation unit and two hydrogen membrane separation units are utilized.
摘要翻译: 本发明提供了一种更有效地回收氢气和二氧化碳的方法,优选至少50%,甚至更优选至少75%,最优选至少90%的二氧化碳。 本发明还提供了从合成气中捕集至少80%的二氧化碳的设计,其允许在合成气中同时生产中等至大量的氢气作为在氢气发生设备中氢的生产的一部分。 通过使用本发明的方法,特别是在氢气发生装置方面,可以通过平衡来自氢气分离器的富氢渗透物的循环来增加氢气的回收和合成气流中二氧化碳的捕获 当利用二氧化碳分离单元,二氧化碳膜分离单元和两个氢膜分离单元时,单位到处理单元和/或容量允许的水煤气变化。
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公开(公告)号:US20120291482A1
公开(公告)日:2012-11-22
申请号:US13169191
申请日:2011-06-27
申请人: Paul Terrien , Trapti Chaubey , Purushottam V. Shanbhag , Bhadra S. Grover , Dennis A. Vauk , Arthur Darde , Pascal Marty
发明人: Paul Terrien , Trapti Chaubey , Purushottam V. Shanbhag , Bhadra S. Grover , Dennis A. Vauk , Arthur Darde , Pascal Marty
IPC分类号: F25J3/08
CPC分类号: C01B3/38 , C01B3/36 , C01B3/384 , C01B3/48 , C01B3/501 , C01B3/506 , C01B3/56 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/0283 , C01B2203/0288 , C01B2203/0294 , C01B2203/0405 , C01B2203/043 , C01B2203/046 , C01B2203/0475 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/146 , C01B2203/147 , C01B2203/148 , C01B2203/86 , F25J3/0223 , F25J3/0252 , F25J3/0266 , F25J2200/02 , F25J2205/04 , F25J2205/40 , F25J2205/80 , F25J2210/04 , F25J2220/82 , F25J2230/30 , F25J2245/02 , Y02C10/04 , Y02C10/12 , Y02P20/128 , Y02P20/152 , Y02P30/30
摘要: The present invention provides a process for recovering hydrogen and carbon dioxide from a process stream utilizing a carbon dioxide separation unit and two membrane separation units. The present invention further provides a process within a hydrogen generation plant to increase recovery of hydrogen and capture equal to or greater than 80% of the carbon dioxide in the syngas stream. By using the process of the present invention, especially in terms of a hydrogen generation plant, it is possible to increase recovery of hydrogen and capture of the carbon dioxide in the syngas stream by balancing the recycle of the hydrogen rich permeate from the hydrogen membrane separation unit to the process unit and/or the water gas shift as capacity allows when a carbon dioxide separation unit, a carbon dioxide membrane separation unit and a hydrogen membrane separation unit are utilized.
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公开(公告)号:US20120291481A1
公开(公告)日:2012-11-22
申请号:US13169158
申请日:2011-06-27
申请人: Paul Terrien , Trapti Chaubey , Purushottam V. Shanbhag , Bhadra S. Grover , Dennis A. Vauk , Arthur Darde , Pascal Marty
发明人: Paul Terrien , Trapti Chaubey , Purushottam V. Shanbhag , Bhadra S. Grover , Dennis A. Vauk , Arthur Darde , Pascal Marty
IPC分类号: F25J3/08
CPC分类号: C01B3/38 , C01B3/36 , C01B3/384 , C01B3/48 , C01B3/501 , C01B3/506 , C01B3/56 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/0283 , C01B2203/0288 , C01B2203/0294 , C01B2203/0405 , C01B2203/043 , C01B2203/046 , C01B2203/0475 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/146 , C01B2203/147 , C01B2203/148 , C01B2203/86 , F25J3/0223 , F25J3/0252 , F25J3/0266 , F25J2200/02 , F25J2205/04 , F25J2205/40 , F25J2205/80 , F25J2210/04 , F25J2220/82 , F25J2230/30 , F25J2245/02 , Y02C10/04 , Y02C10/12 , Y02P20/128 , Y02P20/152 , Y02P30/30
摘要: The present invention provides a process for recovering hydrogen and carbon dioxide from a process stream utilizing a carbon dioxide separation unit and two membrane separation units. The present invention further provides a process within a hydrogen generation plant to increase recovery of hydrogen and capture equal to or greater than 80% of the carbon dioxide in the syngas stream. By using the process of the present invention, especially in terms of a hydrogen generation plant, it is possible to increase recovery of hydrogen and capture of the carbon dioxide in the syngas stream by balancing the recycle of the hydrogen rich permeate from the hydrogen membrane separation unit to the process unit and/or the water gas shift as capacity allows when a carbon dioxide separation unit, a carbon dioxide membrane separation unit and a hydrogen membrane separation unit are utilized.
摘要翻译: 本发明提供一种利用二氧化碳分离单元和两个膜分离单元从工艺流中回收氢和二氧化碳的方法。 本发明进一步提供氢气发生设备内的一种方法,以增加氢气的回收并捕获等于或大于合成气流中二氧化碳的80%。 通过使用本发明的方法,特别是在氢气发生装置方面,可以通过平衡来自氢气分离器的富氢渗透物的循环来增加氢的回收和合成气流中的二氧化碳的捕获 当使用二氧化碳分离单元,二氧化碳膜分离单元和氢分离单元时,容量允许的单位到处理单元和/或水煤气变化。
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公开(公告)号:US20120291483A1
公开(公告)日:2012-11-22
申请号:US13169206
申请日:2011-06-27
申请人: Paul Terrien , Trapti Chaubey , Purushottam V. Shanbhag , Bhadra S. Grover , Dennis A. Vauk , Arthur Darde , Pascal Marty
发明人: Paul Terrien , Trapti Chaubey , Purushottam V. Shanbhag , Bhadra S. Grover , Dennis A. Vauk , Arthur Darde , Pascal Marty
IPC分类号: F25J3/08
CPC分类号: C01B3/38 , C01B3/36 , C01B3/384 , C01B3/48 , C01B3/501 , C01B3/506 , C01B3/56 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/0283 , C01B2203/0288 , C01B2203/0294 , C01B2203/0405 , C01B2203/043 , C01B2203/046 , C01B2203/0475 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/146 , C01B2203/147 , C01B2203/148 , C01B2203/86 , F25J3/0223 , F25J3/0252 , F25J3/0266 , F25J2200/02 , F25J2205/04 , F25J2205/40 , F25J2205/80 , F25J2210/04 , F25J2220/82 , F25J2230/30 , F25J2245/02 , Y02C10/04 , Y02C10/12 , Y02P20/128 , Y02P20/152 , Y02P30/30
摘要: The present invention provides a process for recovering hydrogen and carbon dioxide from a process stream utilizing a carbon dioxide separation unit and two membrane separation units. The present invention further provides a process within a hydrogen generation plant to increase recovery of hydrogen and capture equal to or greater than 80% of the carbon dioxide in the syngas stream. By using the process of the present invention, especially in terms of a hydrogen generation plant, it is possible to increase recovery of hydrogen and capture of the carbon dioxide in the syngas stream by balancing the recycle of the hydrogen rich permeate from the hydrogen membrane separation unit to the process unit and/or the water gas shift as capacity allows when a carbon dioxide separation unit, a carbon dioxide membrane separation unit and a hydrogen membrane separation unit are utilized.
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公开(公告)号:US20110126459A1
公开(公告)日:2011-06-02
申请号:US13056024
申请日:2009-07-23
IPC分类号: C01B3/32
CPC分类号: F25J3/0223 , C01B3/382 , C01B3/384 , C01B2203/0233 , C01B2203/0244 , C01B2203/0415 , C01B2203/042 , C01B2203/046 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2203/0811 , C01B2203/1241 , C01B2203/1258 , C01B2203/147 , C01B2203/148 , F25J3/0233 , F25J3/0252 , F25J3/0261 , F25J2205/30 , F25J2205/40 , F25J2205/60 , F25J2215/02 , F25J2230/60 , F25J2235/60 , F25J2245/02
摘要: A method for generating and purifying syngas and to an apparatus for generating and purifying syngas is presented.
摘要翻译: 提出了一种产生和净化合成气的方法,以及用于产生和净化合成气的装置。
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公开(公告)号:US08888873B2
公开(公告)日:2014-11-18
申请号:US13056024
申请日:2009-07-23
IPC分类号: B01J7/00
CPC分类号: F25J3/0223 , C01B3/382 , C01B3/384 , C01B2203/0233 , C01B2203/0244 , C01B2203/0415 , C01B2203/042 , C01B2203/046 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2203/0811 , C01B2203/1241 , C01B2203/1258 , C01B2203/147 , C01B2203/148 , F25J3/0233 , F25J3/0252 , F25J3/0261 , F25J2205/30 , F25J2205/40 , F25J2205/60 , F25J2215/02 , F25J2230/60 , F25J2235/60 , F25J2245/02
摘要: A method for generating and purifying syngas and to an apparatus for generating and purifying syngas is presented.
摘要翻译: 在产生和净化合成气的过程中,在提供有进料气体和燃料的发生单元中产生含有氢气,一氧化碳和甲烷的合成气,合成气在分离单元中纯化,以产生至少一种 用一氧化碳或氢气富集的液体和至少一种甲烷富集流体,在与进料气体或与该方法的富氢气体混合之后,富含甲烷的流体被加压,并且至少一个 混合物的一部分被送到发生单元。
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