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公开(公告)号：EP0016631B2
公开(公告)日：1986-12-03
申请号：EP80300826.7
申请日：1980-03-19
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公开(公告)号：EP0052482B1
公开(公告)日：1984-03-14
申请号：EP81305364.2
申请日：1981-11-12
CPC分类号： F25J3/0266 , B01D53/1406 , B01D53/1418 , B01D53/1462 , C01B3/52 , C01B32/50 , C01B2203/0415 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2203/0485 , F25J3/0223 , F25J3/0252 , F25J3/08 , F25J2200/04 , F25J2200/74 , F25J2200/78 , F25J2205/40 , F25J2205/50 , F25J2205/60 , F25J2220/82 , F25J2220/84 , F25J2260/80 , Y02C10/06 , Y02C10/12 , Y02P20/152 , Y10S62/928 , Y10S62/931
摘要： This invention relates to a method for producing a hydrogen stream and a carbon dioxide stream from a mixed gas feedstock containing hydrogen, carbon dioxide, and contaminant sulfur compounds. The method comprises scrubbing the gas feedstock with a carbon dioxide laden solvent in an initial scrubbing zone under conditions such that not more than 70% of the carbonyl sulfide in the feedstock is removed in the initial zone, physically scrubbing the initially scrubbed feedstock with a solvent under conditions sufficient for removing substantially all the carbon dioxide and carbonyl sulfide therefrom to leave a pure hydrogen stream desorbing carbon dioxide and carbonyl sulfide and other gases from the liquid from the second scrubbing zone and then fractionating the resultant carbon dioxide stream containing hydrogen, carbon oxides, etc. to produce said carbon dioxide stream for use in urea synthesis.
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3.发明公开Integrated production of fuel gas and oxygenated organic compounds from synthesis gas 失效用于生产燃料气体和含氧有机产品的集成过程。
公开(公告)号：EP0609813A1
公开(公告)日：1994-08-10
申请号：EP94101419.3
申请日：1994-01-31
IPC分类号： C07C1/04
CPC分类号： C07C29/1516 , C07C27/06 , C07C41/01 , C07C31/04 , C07C43/043
摘要： An oxygenated organic liquid product and a fuel gas are produced from a portion of synthesis gas comprising hydrogen, carbon monoxide, carbon dioxide, and sulfur-containing compounds in a integrated feed treatment and catalytic reaction system. To prevent catalyst poisoning, the sulfur-containing compounds in the reactor feed are absorbed in a liquid comprising the reactor product, and the resulting sulfur-containing liquid is regenerated by stripping with untreated synthesis gas from the reactor. Stripping offgas is combined with the remaining synthesis gas to provide a fuel gas product. A portion of the regenerated liquid is used as makeup to the absorber and the remainder is withdrawn as a liquid product. The method is particularly useful for integration with a combined cycle coal gasification system utilizing a gas turbine for electric power generation.
摘要翻译： 含氧的有机液体产物和燃料气体从合成气包含氢气，一氧化碳，二氧化碳，和含硫化合物中的一个集成的进料处理和催化反应体系中的部分中产生。为防止催化剂中毒，该含硫 反应器进料中的化合物被吸收在包括反应器产物的液体，并将得到的含硫液体被从反应器中，与未处理的合成气汽提再生。 汽提废气与其余的合成气组合，以提供燃料气体产物。 再生液体的一部分被用作化妆到吸收器，而剩余部分作为液体取出产物。 该方法是用于与煤气化联合循环系统利用用于发电的燃气涡轮机的集成特别有用。
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4.发明公开Oxygen recovery from turbine exhaust using solid electrolyte membrane 失效Gewinnung von Sauerstoff aus Turbinenabgas unter Verwendung von fester Elektrolytmembran。
公开(公告)号：EP0458217A2
公开(公告)日：1991-11-27
申请号：EP91108059.6
申请日：1991-05-17
CPC分类号： B01D53/326 , C01B13/0251 , C01B2210/0046
摘要： A process is provided for extracting high purity oxygen from gas turbine exhaust streams by passing the gas turbine exhaust over the feed side of solid electrolyte membrane selective to the permeation of oxygen over other components of the exhaust stream to separate the oxygen from the exhaust stream, and removing the oxygen product stream from the permeate side of the membrane.
摘要翻译： 提供了一种用于通过使燃气涡轮机废气在固体电解质膜的进料侧上通过氧气渗透到排气流的其它组分上而选择性地从燃气轮机废气流中提取高纯度氧以将废气流分离出来的方法， 并从膜的渗透侧除去氧产物流。
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公开(公告)号：EP0195447B1
公开(公告)日：1989-10-18
申请号：EP86103797.6
申请日：1986-03-20
IPC分类号： C01B17/04
CPC分类号： C01B17/0413
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6.发明公开Method for controlling fluidized catalytic cracker regenerator temperature and velocity with carbon dioxide 失效Methode zur Kontrolle der Temperatur und Fliessgeschwindigkeit eines FCC-Regenerators mittels Carbondioxids。
公开(公告)号：EP0152845A1
公开(公告)日：1985-08-28
申请号：EP85101084.3
申请日：1985-02-01
发明人： Hegarty, William Patrick , Liebelson, Michael Solomon , Bronfenbrenner, James Cole , Taschler, David Robert , Rao, Pradip
CPC分类号： C10G11/182 , C10G11/187 , Y02P30/446
摘要： A process is set forth for the operation and control of a fluidized catalytic cracking unit wherein the regenerator is fed witz independently controlled oxygen rich gas and carbon dioxide rich gas to maintain desired temperatures, velocities, and catalyst to oil (C/O) ratio within the constraints of the system.
摘要翻译： 阐述了流化催化裂化装置的操作和控制的过程，其中再生器被独立控制的富氧气体和富含二氧化碳的气体进料，以保持所需的温度，速度和催化剂与油（C / O）的比例 系统的约束。
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7.发明授权Integrated production of fuel gas and oxygenated organic compounds from synthesis gas 失效含氧用于生产燃料气体和的集成过程的有机产品
公开(公告)号：EP0609813B1
公开(公告)日：1997-11-05
申请号：EP94101419.3
申请日：1994-01-31
IPC分类号： C07C1/04
CPC分类号： C07C29/1516 , C07C27/06 , C07C41/01 , C07C31/04 , C07C43/043
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8.发明公开
公开(公告)号：EP0458217A3
公开(公告)日：1992-11-25
申请号：EP91108059.6
申请日：1991-05-17
CPC分类号： B01D53/326 , C01B13/0251 , C01B2210/0046
摘要： A process is provided for extracting high purity oxygen from gas turbine exhaust streams by passing the gas turbine exhaust over the feed side of solid electrolyte membrane selective to the permeation of oxygen over other components of the exhaust stream to separate the oxygen from the exhaust stream, and removing the oxygen product stream from the permeate side of the membrane.
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9.发明授权
公开(公告)号：EP0162251B1
公开(公告)日：1988-07-13
申请号：EP85104082.4
申请日：1985-04-03
CPC分类号： F25J3/04533 , B01J8/26 , B01J29/90 , C10G11/182 , C10G11/185 , F25J3/04527 , F25J3/04563 , Y02P20/129 , Y02P30/446
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10.发明公开
公开(公告)号：EP0170244A2
公开(公告)日：1986-02-05
申请号：EP85109502.6
申请日：1985-07-29
IPC分类号： C01B13/02
CPC分类号： B01D53/22 , B01D53/0462 , B01D53/047 , B01D53/326 , B01D2256/10 , B01D2256/12 , B01D2257/104 , F02C6/10 , Y02E20/16 , Y02P20/129
摘要： A method is set forth for the generation of net power and the recovery of by-product oxygen-enriched gas at low power requirements. Air is compressed to elevated temperature and pressure, at least a portion of the air is combusted and a portion of the oxygen is removed from the air or combustion effluent through a membrane or adsorbent before the oxygen lean combustion effluent is expanded through a turbine to recover power for the process and net power.
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