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公开(公告)号：US06669744B2
公开(公告)日：2003-12-30
申请号：US10301953
申请日：2002-11-22
申请人： Rodney John Allam , Rebecca Cotton
发明人： Rodney John Allam , Rebecca Cotton
IPC分类号： C01B332
CPC分类号： C01B3/38 , C01B3/382 , C01B13/0229 , C01B2203/0233 , C01B2203/0244 , C01B2203/0261 , C01B2203/0283 , C01B2203/061 , C01B2203/062 , C01B2203/0833 , C01B2203/0844 , C01B2203/0883 , C01B2203/0894 , C01B2203/1241 , C01B2203/141 , C01B2203/142 , C01B2203/148 , C01B2203/82 , C01B2203/84 , C01B2210/0046 , F25J3/04539 , F25J3/04575 , F25J3/04593 , F25J3/04612 , F25J2240/80
摘要： A process for the production of synthesis gas from a hydrocarbon fuel and steam and/or oxygen gas wherein at least part of any steam requirement is provided by heat exchange against exhaust gas from a gas turbine driving an air separation unit supplying at least part of any oxygen requirement for the synthesis gas production. The process is particularly applicable when the synthesis gas is used to prepare a synfuel by methanol synthesis or a Fischer-Tropsch process.
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公开(公告)号：US06615589B2
公开(公告)日：2003-09-09
申请号：US09965969
申请日：2001-09-27
申请人： Rodney John Allam , Rebecca Cotton
发明人： Rodney John Allam , Rebecca Cotton
IPC分类号： F02C328
CPC分类号： F01K23/067 , F01K23/064 , Y02E20/18
摘要： A process for generating power from the expansion of steam in a steam turbine system. The steam is generated by at least partially vaporizing pre-heated water by heat exchange against a first fuel gas that is generated exothermically. The at least partially vaporized water is then heated to produce the steam by heat exchange against expanded combustion product gas that is generated by the combustion of a second fuel gas in the presence of compressed oxygen-containing gas and the subsequent expansion of the combustion product gas. The steam is then expanded in a steam turbine system having more than one pressure stage to produce power and an expanded steam stream.
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公开(公告)号：US5779767A
公开(公告)日：1998-07-14
申请号：US814749
申请日：1997-03-07
CPC分类号： B01J20/183 , B01D53/04 , B01D53/0462 , B01J20/08 , B01D2253/104 , B01D2253/108 , B01D2253/1085 , B01D2253/30 , B01D2257/404 , B01D2257/504 , B01D2257/7022 , B01D2257/80 , B01D2259/416 , B01D53/047 , B01J2220/42 , Y02C10/08 , Y10S95/902
摘要： A process for the adsorption of at least carbon dioxide, water and oxides of nitrogen and preferably acetylene from a feed gas, comprises contacting the feed gas with an adsorbent mixture of a zeolite and an alumina. The process may be operated as a swing adsorption process comprising contacting the gas with the adsorbent at a first temperature and pressure to adsorb at least carbon dioxide, water and oxides of nitrogen therefrom and periodically regenerating the adsorbent by reducing the pressure and or increasing the temperature to which the adsorbent is exposed.
摘要翻译： 至少吸附二氧化碳，水和氮气氧化物，优选来自进料气体的乙炔的方法包括使进料气体与沸石和氧化铝的吸附剂混合物接触。 该方法可以作为变形吸附方法进行操作，包括在第一温度和压力下使气体与吸附剂接触以吸附至少二氧化碳，水和氮氧化物，并通过降低压力和/或增加温度来周期性地再生吸附剂 吸附剂暴露在其上。
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公开(公告)号：US08257476B2
公开(公告)日：2012-09-04
申请号：US12884470
申请日：2010-09-17
申请人： Vincent White , Rodney John Allam
发明人： Vincent White , Rodney John Allam
IPC分类号： B01D53/14
CPC分类号： F25J3/0266 , C01B32/50 , F25J3/0223 , F25J3/0252 , F25J2200/02 , F25J2200/70 , F25J2200/76 , F25J2205/04 , F25J2210/04 , F25J2210/70 , F25J2220/82 , F25J2230/06 , F25J2230/32 , F25J2230/80 , F25J2240/90 , F25J2245/02 , F25J2270/02 , Y02C10/06 , Y02C10/12 , Y02P20/129 , Y02P20/152
摘要： A first contaminant selected from oxygen and carbon monoxide is removed from impure liquid carbon dioxide using a mass transfer separation column system which is reboiled by indirect heat exchange against crude carbon dioxide fluid, the impure liquid carbon dioxide having a greater concentration of carbon dioxide than the crude carbon dioxide fluid. The invention has particular application in the recovery of carbon dioxide from flue gas generated in an oxyfuel combustion process or waste gas from a hydrogen PSA process. Advantages include reducing the level of the first contaminant to not more than 1000 ppm.
摘要翻译： 使用传质分离柱系统从不纯的液体二氧化碳中除去选自氧气和一氧化碳的第一污染物，该系统通过与粗二氧化碳流体的间接热交换而再沸腾，不纯的液态二氧化碳比二氧化碳浓度高 粗二氧化碳流体。 本发明特别适用于在氧燃料燃烧过程中生成的烟道气中回收二氧化碳或来自氢PSA过程的废气。 优点包括将第一污染物的水平降低到不超过1000ppm。
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公开(公告)号：US08091369B2
公开(公告)日：2012-01-10
申请号：US12171699
申请日：2008-07-11
IPC分类号： F22G3/00
CPC分类号： F01K3/24 , F01K7/22 , F01K23/10 , Y02E20/16 , Y02E20/326 , Y02E20/344
摘要： A superheater in a power plant that superheats steam to operation conditions exceeding an operating limit of an associated steam-producing boiler. The superheater combusts oxygen and fuel with cooled recycled combustion gas to produce a CO2-rich combustion product gas stream at a fixed temperature. The combustion gas is used as the heat transfer fluid in the superheater's heat exchanger. The CO2-rich flue gas stream allows for efficient capture of substantially pure CO2. The superheater may be retrofitted to an existing power plant as a separate component, external to the boiler. The plant may thus have its electrical power output increased, while its overall CO2 emissions per nit of generated power is decreased, even when inexpensive, readily-available fossil fuels are used as the primary fuel for filing the boiler and/or the superheater.
摘要翻译： 发电厂的过热器将蒸汽过热至运行条件超过相关蒸汽生产锅炉的运行极限。 过热器通过冷却的循环燃烧气体燃烧氧气和燃料，以在固定温度下产生富CO 2的燃烧产物气流。 燃烧气体用作过热器热交换器中的传热流体。 富二氧化碳的烟气流允许有效捕获基本上纯的二氧化碳。 过热器可以作为锅炉外部的单独组件改装到现有发电厂。 因此，即使使用廉价的，易于使用的化石燃料作为用于归档锅炉和/或过热器的主要燃料，工厂可以增加其电力输出，同时其产生的功率的总体二氧化碳排放量减少。
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公开(公告)号：US08088196B2
公开(公告)日：2012-01-03
申请号：US11656913
申请日：2007-01-23
申请人： Vincent White , Rodney John Allam
发明人： Vincent White , Rodney John Allam
IPC分类号： B01D53/22
CPC分类号： F23J15/006 , B01D53/002 , B01D53/22 , B01D53/229 , B01D63/02 , B01D63/08 , B01D63/10 , B01D2257/504 , B01D2313/12 , B01D2313/38 , C01B32/50 , F23J2215/50 , F23J2219/70 , F23L7/007 , F23L2900/07001 , F25J3/0266 , F25J3/067 , F25J2200/02 , F25J2200/70 , F25J2200/76 , F25J2205/04 , F25J2205/40 , F25J2205/80 , F25J2210/70 , F25J2220/82 , F25J2230/30 , F25J2230/32 , F25J2230/80 , F25J2240/90 , F25J2245/02 , F25J2270/02 , Y02C10/04 , Y02C10/10 , Y02C10/12 , Y02E20/322 , Y02E20/326 , Y02E20/344 , Y02P20/152
摘要： Carbon dioxide and oxygen are separated from a feed gas, preferably derived from flue gas from an oxyfuel combustion process, by diffusion across at least one membrane in a membrane separation system to produce separated carbon dioxide gas comprising oxygen, which is fed to the oxyfuel combustion process to improve the performance of the process.
摘要翻译： 将二氧化碳和氧气从源自氧燃料燃烧过程的烟气中的进料气体分离，通过在膜分离系统中的至少一个膜扩散以产生包含氧气的分离的二氧化碳气体，其被供给到氧燃料燃烧 过程来提高过程的性能。
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公开(公告)号：US20100007146A1
公开(公告)日：2010-01-14
申请号：US12171699
申请日：2008-07-11
IPC分类号： F01D15/10
CPC分类号： F01K3/24 , F01K7/22 , F01K23/10 , Y02E20/16 , Y02E20/326 , Y02E20/344
摘要： A superheater in a power plant that superheats steam to operation conditions exceeding an operating limit of an associated steam-producing boiler. The superheater combusts oxygen and fuel with cooled recycled combustion gas to produce a CO2-rich combustion product gas stream at a fixed temperature. The combustion gas is used as the heat transfer fluid in the superheater's heat exchanger. The CO2-rich flue gas stream allows for efficient capture of substantially pure CO2. The superheater may be retrofitted to an existing power plant as a separate component, external to the boiler. The plant may thus have its electrical power output increased, while its overall CO2 emissions per nit of generated power is decreased, even when inexpensive, readily-available fossil fuels are used as the primary fuel for filing the boiler and/or the superheater.
摘要翻译： 发电厂的过热器将蒸汽过热至运行条件超过相关蒸汽生产锅炉的运行极限。 过热器通过冷却的循环燃烧气体燃烧氧气和燃料，以在固定温度下产生富CO 2的燃烧产物气流。 燃烧气体用作过热器热交换器中的传热流体。 富二氧化碳的烟气流允许有效捕获基本上纯的二氧化碳。 过热器可以作为锅炉外部的单独组件改装到现有发电厂。 因此，即使使用廉价的，易于使用的化石燃料作为用于归档锅炉和/或过热器的主要燃料，工厂可以增加其电力输出，同时其产生的功率的总体二氧化碳排放量减少。
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公开(公告)号：US20080173585A1
公开(公告)日：2008-07-24
申请号：US11656922
申请日：2007-01-23
申请人： Vincent White , Rodney John Allam
发明人： Vincent White , Rodney John Allam
IPC分类号： B01D15/08
CPC分类号： F25J3/0266 , B01D53/002 , B01D53/047 , B01D2256/16 , C01B32/50 , F25J2200/02 , F25J2200/40 , F25J2200/70 , F25J2200/76 , F25J2200/78 , F25J2205/02 , F25J2205/04 , F25J2210/04 , F25J2210/70 , F25J2215/04 , F25J2220/82 , F25J2240/90 , F25J2245/02 , F25J2270/02 , F25J2270/88 , Y02C10/12 , Y02P20/152 , Y10S62/926 , Y10S62/928
摘要： Impure carbon dioxide (“CO2”) comprising a first contaminant selected from the group consisting of oxygen (“O2”) and carbon monoxide (“CO”) is purified by separating expanded impure carbon dioxide liquid in a mass transfer separation column system. The impure carbon dioxide may be derived from, for example, flue gas from an oxyfuel combustion process or waste gas from a hydrogen (“H2”) PSA system.
摘要翻译： 包含选自氧（“O 2”）和一氧化碳（“CO”）的第一污染物的不纯的二氧化碳（“CO 2”）被纯化 通过在传质分离柱系统中分离膨胀的不纯二氧化碳液体。 不纯的二氧化碳可以衍生自例如来自氧燃料燃烧过程的烟道气或来自氢气（“H 2”）的PSA系统的废气。
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公开(公告)号：US5846295A
公开(公告)日：1998-12-08
申请号：US812564
申请日：1997-03-07
CPC分类号： F25J3/04169 , B01D53/0407 , B01D53/0462 , F25J3/04157 , F25J3/04181 , F25J3/04775 , B01D2253/104 , B01D2253/108 , B01D2257/504 , B01D2257/702 , B01D2257/80 , B01D2259/40052 , B01D2259/402 , F25J2205/70 , F25J2230/04 , Y02C10/08
摘要： Temperature swing adsorption to remove CO.sub.2 from a gas stream is conducted using alumina to adsorb all the water and at least most of the carbon dioxide from the gas stream. Optionally a downstream zone of zeolite may be provided to remove further carbon dioxide and hydrocarbons.
摘要翻译： 使用氧化铝进行从气流中除去CO 2的温度变化吸附以吸附来自气流的所有水和至少大部分二氧化碳。 任选地，可以提供沸石的下游区以除去进一步的二氧化碳和烃。
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