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22 条记录 (耗时 0.031 秒)

    Process For The Production Of Hydrogen And Carbon Dioxide
    1.
    发明申请
    Process For The Production Of Hydrogen And Carbon Dioxide 审中-公开

    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.

    Process For The Production Of Hydrogen And Carbon Dioxide
    3.
    发明申请
    Process For The Production Of Hydrogen And Carbon Dioxide 审中-公开

    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.

    Process For The Production Of Hydrogen And Carbon Dioxide
    4.
    发明申请
    Process For The Production Of Hydrogen And Carbon Dioxide 审中-公开
    氢和二氧化碳生产工艺

    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。

    Drying Process For Flue Gas Treatment
    10.
    发明申请
    Drying Process For Flue Gas Treatment 审中-公开
    烟气处理干燥过程

    公开(公告)号：US20120145000A1

    公开(公告)日：2012-06-14

    申请号：US12965056

    申请日：2010-12-10

    申请人： Trapti Chaubey ,  Jean-Pierre Tranier ,  Paul Terrien

    发明人： Trapti Chaubey ,  Jean-Pierre Tranier ,  Paul Terrien

    IPC分类号： B01D53/02

    CPC分类号： B01D53/261 ,  B01D53/002 ,  B01D53/06 ,  B01D2253/106 ,  B01D2253/116 ,  B01D2256/22 ,  B01D2257/504 ,  B01D2257/80 ,  B01D2258/0283 ,  B01D2259/4009 ,  Y02C10/08

    摘要： An apparatus and method for drying a moist gas is provided. The apparatus includes a revolving desiccant rotor with at least an adsorption sector and a regeneration chamber; the regeneration chamber comprising at least a first dry gas sector, a hot regeneration sector, and a second dry gas sector, and optionally a cold regeneration sector. The method includes at least an adsorption sector and a regeneration chamber; the regeneration chamber comprising at least a first dry gas sector, a hot regeneration sector, and a second dry gas sector, and optionally a cold regeneration sector. This method includes the steps of; contacting a moist gas stream with the desiccant in the adsorption sector, thereby producing a dry gas stream; contacting a first dry gas stream with the desiccant in the first dry gas sector, thereby producing a first wet gas stream; contacting a hot partially wet gas stream with the desiccant in the hot regeneration sector, thereby producing a warm wet gas stream; contacting a dry regeneration gas stream with the desiccant in the second dry gas sector, thereby producing a wet regeneration gas stream, and contacting a regeneration purge gas stream with the desiccant in the cold regeneration sector, thereby producing a warm purge gas stream.

    摘要翻译： 提供了一种用于干燥潮湿气体的装置和方法。 该装置包括至少具有吸附扇区和再生室的旋转干燥剂转子; 所述再生室包括至少第一干燥气体部分，热再生部分和第二干燥气体部分，以及任选的冷再生部分。 该方法至少包括吸附扇区和再生室; 所述再生室包括至少第一干燥气体部分，热再生部分和第二干燥气体部分，以及任选的冷再生部分。 该方法包括以下步骤： 使湿气流与吸附部分中的干燥剂接触，从而产生干燥气流; 使第一干燥气流与第一干燥气体区段中的干燥剂接触，从而产生第一湿气流; 使热的部分湿气流与热再生扇区中的干燥剂接触，从而产生温暖的湿气流; 使干再生气体流与第二干燥气体区段中的干燥剂接触，从而产生湿再生气流，并使再生吹扫气流与冷再生扇区中的干燥剂接触，从而产生热的吹扫气流。