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1.发明授权
公开(公告)号：US5174866A
公开(公告)日：1992-12-29
申请号：US834733
申请日：1992-02-12
申请人： Michael S. Chen , William P. Hegarty , William A. Steyert, deceased , by Lila O. Steyer, executrix
发明人： Michael S. Chen , William P. Hegarty , William A. Steyert, deceased , by Lila O. Steyer, executrix
CPC分类号： C01B13/0251 , B01D53/326 , C01B2210/0046
摘要： A process is provided for extracting high purity oxygen from a gas generator turbine exhaust stream by passing the 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. The reject exhaust stream is then passed through a power generating turbine to recover net power.
摘要翻译： 提供了一种用于通过将涡轮机排气通过固体电解质膜的进料侧的选择性地将氧气渗透到排气流的其它组分上以从排气流中分离氧气的方式从气体发生器涡轮排气流中提取高纯度氧气的过程 并且从膜的渗透侧除去氧产物流。 废弃废气流然后通过发电涡轮机以恢复净功率。
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2.发明授权
公开(公告)号：US5118395A
公开(公告)日：1992-06-02
申请号：US529093
申请日：1990-05-24
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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公开(公告)号：US4826670A
公开(公告)日：1989-05-02
申请号：US714146
申请日：1985-03-20
申请人： William P. Hegarty
发明人： William P. Hegarty
CPC分类号： C01B17/0413
摘要： A process and system are set forth for improving an oxygen-enriched Claus process by introducing a sulfuric acid stream into the reaction furnace to moderate oxygen-induced high temperatures which allow oxygen-enrichment and attendant throughput in the Claus process to higher levels than heretobefore practiced.
摘要翻译： 阐述了一种方法和系统，用于通过将硫酸流引入反应炉中来调节氧气诱导的高温，从而改善富氧克劳斯方法，这使得克劳斯方法中的富氧和合格的生产量比以前实施的水平高 。
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4.发明授权
公开(公告)号：US5375580A
公开(公告)日：1994-12-27
申请号：US118542
申请日：1993-09-08
CPC分类号： F02M21/0287 , F02B29/0443 , F02M21/0245 , F02M21/029 , F02M21/06 , F02B2275/14 , F02M21/0209 , F02M21/0212 , F02M21/0215 , F02M21/0275 , Y02T10/123 , Y02T10/146 , Y02T10/32
摘要： A turbocharged or supercharged internal combustion motive system for utilization of gaseous fuel stored as a liquid wherein the liquefied gaseous fuel is vaporized and warmed at least partially with heat removed from the compressed intake combustion air in the turbocharger or supercharger aftercooler. In a preferred embodiment, the compressed intake combustion air is first cooled in an aftercooler against an ambiently cooled coolant and is subsequently cooled in further aftercooler heat exchange passages against an intermediate coolant which transfers heat removed from the compressed intake combustion air to the liquefied gaseous fuel. Embodiments are disclosed wherein the saturated liquefied gaseous fuel is first subcooled and then pumped to pressures high enough for direct combustion chamber injection and another embodiment discloses vaporization of the saturated liquefied gaseous fuel with compression of the vaporized gas in a compression-type injection system or by low pressure carburetion into the internal combustion engine.
摘要翻译： 涡轮增压或增压的内燃动机系统，用于利用作为液体储存的气体燃料，其中液化气体燃料至少部分地由涡轮增压器或增压器后冷器中的压缩进气燃烧空气除去的热量被蒸发和加热。 在优选实施例中，压缩的进气燃烧空气首先在后冷却器中冷却到环境冷却的冷却剂上，并随后在进一步的后冷却器热交换通道中冷却中间冷却剂，该中间冷却剂将从压缩的进气燃烧空气中移出的热传递到液化气体燃料 。 公开了实施例，其中饱和液化气体燃料首先被过冷却然后被泵送到足够高的压力以用于直接燃烧室注射，并且另一个实施方案公开了饱和液化气体燃料在压缩型注射系统中压缩气化气体或通过 低压化油进入内燃机。
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5.发明授权
公开(公告)号：US5240476A
公开(公告)日：1993-08-31
申请号：US579123
申请日：1990-09-07
申请人： William P. Hegarty
发明人： William P. Hegarty
CPC分类号： C10G70/048 , B01D53/1418 , B01D53/1425 , C01B17/167 , C10L3/00 , Y02P20/131
摘要： A process for recovery of hydrogen sulfide-free fuel, while maintaining desirable carbon dioxide for combustion in a gas turbine to recover power in an integrated gasification combined cycle power plant and obtaining a rich hydrogen sulfide Claus plant feed gas is described.
摘要翻译： 描述了一种用于回收无硫化氢的燃料的方法，同时保持用于燃气轮机中的燃烧所需的二氧化碳以在一体式气化联合循环发电厂中回收功率并获得富硫硫化氢Claus工厂进料气体。
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6.发明授权Low energy process for separating carbon dioxide and acid gases from a carbonaceous off-gas 失效用于从碳质废气中分离二氧化碳和酸性气体的低能量过程
公开(公告)号：US4449994A
公开(公告)日：1984-05-22
申请号：US339359
申请日：1982-01-15
CPC分类号： F25J3/067 , F25J3/0219 , F25J3/0247 , F25J3/0266 , F25J3/04527 , F25J3/062 , F25J3/065 , F25J2200/02 , F25J2200/74 , F25J2210/12 , F25J2210/70 , F25J2220/82 , F25J2230/04 , F25J2230/30 , F25J2260/80 , F25J2270/02 , F25J2270/04 , Y02C10/12 , Y10S62/929
摘要： A process is disclosed for the separation of carbon dioxide and sulfide gases from oil shale retort off-gases, coal gasification off-gases, oxygen fire-flooding or carbon dioxide miscible flood enhanced oil recovery off-gases for recycle to a retort, gasifier or petroleum reservoir or alternately delivery to another process. The process separates the off-gases into an essentially sulfur-free fuel gas and an acid gas for recycle to such a retort, gasifier or reservoir wherein the off-gas is compressed if necessary and cooled to separate the two streams, the acid gas is expanded in an auto refrigeration step to provide the necessary process refrigeration and the acid gas is then recycled to such a retort, gasifier or reservoir. In the oil shale retorting and coal gasification applications, the gas' sulfur constituents are sorbed on spent oil shale particles or coal ash.
摘要翻译： 公开了一种用于将二氧化碳和硫化物气体从油页岩蒸馏废气，煤气化废气，氧气灭火或二氧化碳可混溶的洪水强化油回收废气中分离出来再循环到蒸馏器，气化器或 石油储层或交替输送到另一个过程。 该方法将废气分解成基本上不含硫的燃料气体和用于再循环到这种蒸馏器，气化器或储存器中的酸性气体，其中如果需要，则废气被压缩并冷却以分离两股物流，酸性气体是 在自动制冷步骤中膨胀以提供必要的工艺制冷，然后将酸性气体再循环到这种蒸馏器，气化器或储存器中。 在油页岩蒸馏和煤气化应用中，气体硫成分吸附在废油页岩颗粒或煤灰上。
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公开(公告)号：US5137550A
公开(公告)日：1992-08-11
申请号：US691929
申请日：1991-04-26
申请人： William P. Hegarty , Thomas C. Bono
发明人： William P. Hegarty , Thomas C. Bono
IPC分类号： B01D53/14
CPC分类号： B01D53/1406 , B01D53/1418
摘要： The present invention relates to an improvement to a process for the removal of acid gases from a feed stream containing acid gases in which the feed gas is cooled and countercurrently contacted with a liquid absorbent in an absorber tower and the spent absorbent is regenerated by distillation wherein dissolved acid gases are stripped from the spent absorbent thereby producing a regenerated liquid absorbent and recycled to the absorber tower.The improvement, which is for the production of a product which is essentially free of sulfur containing compounds and has a reduced concentration of carbon dioxide, comprises the following steps: (a) compressing the acid gas-lean product gas to an elevated pressure and cooling the resultant compressed portion; (b) countercurrently contacting the elevated pressure, cooled, acid gas-lean product gas of step (a) and the regenerated liquid absorbent in a second absorber, thereby producing the product, which is essentially free of sulfur containing compounds and has a reduced concentration of carbon dioxide, at the top of the second absorber and a partially spent absorbent at the bottom of the second absorber, wherein said second absorber is operated at a higher pressure than the operating pressure of said absorber tower; (c) recovering the product, which is sulfur containing compounds and has a reduced concentration of carbon dioxide; and (d) using the partially spent absorbent to contact with the feed gas in the absorber tower.
摘要翻译： 本发明涉及从含有酸性气体的进料流中除去酸性气体的方法的改进，其中进料气体被冷却并与吸收塔中的液体吸收剂逆流接触，并且废的吸收剂通过蒸馏再生，其中 溶解的酸性气体从废吸收剂中剥离，从而产生再生液体吸收剂并再循环至吸收塔。 用于生产基本上不含硫化合物并且具有降低的二氧化碳浓度的产品的改进包括以下步骤：（a）将酸性气体贫产物气体压缩至升高的压力和冷却 所得压缩部分; （b）在第二吸收器中使步骤（a）的高压，冷却，酸性贫气产物气体和再生液体吸收剂逆流接触，从而产生基本上不含硫化合物并具有降低的浓度的产物 的第二吸收器的顶部处的二氧化碳和在第二吸收器的底部的部分消耗的吸收剂，其中所述第二吸收器在比所述吸收塔的操作压力更高的压力下操作; （c）回收含硫化合物并具有降低的二氧化碳浓度的产物; 和（d）使用部分消耗的吸收剂与吸收塔中的进料气体接触。
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公开(公告)号：US4242108A
公开(公告)日：1980-12-30
申请号：US91882
申请日：1979-11-07
CPC分类号： B01D53/1462 , C01B3/52 , C01B2203/0415 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2203/0485 , Y02C10/06 , Y02P20/152
摘要： A novel method is disclosed for treating a contaminated gas such as a contaminated natural gas or a synthesis product gas from the partial oxidation of petroleum or coal to concentrate and remove hydrogen sulfide at a reduced energy and capital requirement. Hydrogen sulfide in the contaminated stream is absorbed to form a hydrogen sulfide rich solvent which includes co-absorbed carbon dioxide, which is then removed to prevent dilution of the concentrated hydrogen sulfide formed when the solvent is regenerated. The solvent leaving the hydrogen sulfide absorber is heated before entering a high pressure stripper column wherein the co-absorbed carbon dioxide is stripped from the solvent, preferably by stripping with nitrogen or a portion of the product gas, and the carbon dioxide is recycled to the hydrogen sulfide absorber. The CO.sub.2 stripper is operated at a pressure not substantially below the pressure of the hydrogen sulfide absorber, eliminating the need for large compressors required in conventional methods to recycle the carbon dioxide.
摘要翻译： 公开了一种新的方法，用于处理受污染的天然气或来自石油或煤的部分氧化的合成产物气体，以降低能量和资本要求来浓缩和除去硫化氢。 被污染的流中的硫化氢被吸收以形成富含硫化氢的溶剂，其包括共吸收的二氧化碳，然后将其除去，以防止在溶剂再生时形成的浓硫化氢的稀释。 离开硫化氢吸收剂的溶剂在进入高压汽提塔之前被加热，其中共吸附二氧化碳从溶剂中汽提，优选通过用氮气或一部分产物气体汽提，并将二氧化碳再循环至 硫化氢吸收剂。 二氧化碳汽提器的操作压力基本上不低于硫化氢吸收器的压力，消除了对于循环二氧化碳的常规方法所需的大型压缩机的需要。
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9.发明授权Integrated production of fuel gas and oxygenated organic compounds from synthesis gas 失效从合成气中综合生产燃气和含氧有机化合物
公开(公告)号：US5392594A
公开(公告)日：1995-02-28
申请号：US12092
申请日：1993-02-01
IPC分类号： C07C27/06 , C07C29/151 , C07C41/01 , C01B17/05
CPC分类号： C07C29/1516 , C07C27/06 , C07C41/01
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： 在一体化进料处理和催化反应系统中，由包含氢气，一氧化碳，二氧化碳和含硫化合物的合成气的一部分产生氧化有机液体产物和燃料气体。 为了防止催化剂中毒，反应器进料中的含硫化合物被吸收在包含反应器产物的液体中，所得到的含硫液体通过用反应器中未处理的合成气汽提而被再生。 汽提废气与剩余的合成气组合以提供燃料气体产物。 再生液体的一部分用作吸收剂的组成，其余部分作为液体产物取出。 该方法对于与利用燃气轮机进行发电的联合循环煤气化系统的集成特别有用。
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10.发明授权Process for separating carbon dioxide and sulfur-containing gases from a synthetic fuel production process off-gas 失效从合成燃料生产过程废气中分离二氧化碳和含硫气体的方法
公开(公告)号：US4475347A
公开(公告)日：1984-10-09
申请号：US418517
申请日：1982-09-16
CPC分类号： C10K1/16 , B01D53/1456 , B01D53/1493 , F25J3/08 , Y02C10/06 , Y02P20/152 , Y10S62/922 , Y10S62/928
摘要： A process is described for the separation of an off-gas from a synthetic fuels production process, such as oil shale retorting, coal gasification, oxygen fireflooding or carbon dioxide miscible flood enhanced oil recovery, into an essentially sulfur-free, light fuel gas and a sulfur containing carbon dioxide gas. The off-gas is contacted with methanol to remove the sulfur containing gases and is then cooled to separate out a light fuel gas from a predominantly carbon dioxide gas. The carbon dioxide gas is again contacted with the same methanol to scrub the latter of sulfur-containing gas and reabsorb the sulfur onto the carbon dioxide gas. The carbon dioxide gas can then be recycled to the synthetic fuels production process with deposition of the sulfur therein or the gas can be delivered for export with downstream sulfur treatment.
摘要翻译： 描述了一种将废气与合成燃料生产过程（例如油页岩蒸馏，煤气化，氧气喷射或二氧化碳可混合的洪水强化油采收）分离成基本上无硫的轻质燃料气体的方法， 含硫二氧化碳气体。 废气与甲醇接触以除去含硫气体，然后冷却以从主要二氧化碳气体中分离出轻质燃料气体。 二氧化碳气体再次与相同的甲醇接触以洗涤后者的含硫气体并将硫再吸收到二氧化碳气体上。 然后可以将二氧化碳气体再循环到合成燃料生产过程中，其中沉积硫，或者可以通过下游硫处理将气体输送出口。
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