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1. 发明申请

US20090260518A1 CYCLICAL SWING ADSORPTION PROCESSES 有权
标题翻译：循环旋转吸附过程
公开(公告)号：US20090260518A1
公开(公告)日：2009-10-22
申请号：US12106659
申请日：2008-04-21
申请人： Andrew David Wright , Mohammad Ali Kalbassi , Timothy Christopher Golden , Christopher James Raiswell
发明人： Andrew David Wright , Mohammad Ali Kalbassi , Timothy Christopher Golden , Christopher James Raiswell
IPC分类号： B01D46/46 , B01D53/30
CPC分类号： B01D53/0462 , B01D53/047 , B01D2257/504 , B01D2259/40009 , B01D2259/40086 , B01D2259/402 , B01D2259/4146 , Y02C10/08
摘要： The concentration of adsorbate in the feed gas to an on-stream bed of a cyclical swing adsorption process is monitored and the data processed to predict the time required to complete the on-stream mode of that bed and the purge flow rate and/or other regeneration mode operating condition of the concurrently off-stream bed is modified in response to changes in said predicted time whereby the regeneration mode of the off-steam bed is completed at the same time as the on-stream mode of the concurrent on-stream bed.
摘要翻译：监测进料流中循环挥发吸附过程的原料气中的被吸附物质的浓度，并处理数据以预测完成该床的流道模式所需的时间和吹扫流量和/或其它响应于所述预测时间的变化来修改同时离线床的再生模式操作条件，从而与同时的在线床的同时流模式同时完成了蒸汽床的再生模式。

2. 发明授权

US07846237B2 Cyclical swing adsorption processes 有权
标题翻译：循环挥发吸附过程
公开(公告)号：US07846237B2
公开(公告)日：2010-12-07
申请号：US12106659
申请日：2008-04-21
申请人： Andrew David Wright , Mohammad Ali Kalbassi , Timothy Christopher Golden , Christopher James Raiswell
发明人： Andrew David Wright , Mohammad Ali Kalbassi , Timothy Christopher Golden , Christopher James Raiswell
IPC分类号： B01D53/047
CPC分类号： B01D53/0462 , B01D53/047 , B01D2257/504 , B01D2259/40009 , B01D2259/40086 , B01D2259/402 , B01D2259/4146 , Y02C10/08
摘要： The concentration of adsorbate in the feed gas to an on-stream bed of a cyclical swing adsorption process is monitored and the data processed to predict the time required to complete the on-stream mode of that bed and the purge flow rate and/or other regeneration mode operating condition of the concurrently off-stream bed is modified in response to changes in said predicted time whereby the regeneration mode of the off-steam bed is completed at the same time as the on-stream mode of the concurrent on-stream bed.
摘要翻译：监测进料流中循环挥发吸附过程的原料气中的被吸附物质的浓度，并处理数据以预测完成该床的流道模式所需的时间和吹扫流量和/或其它响应于所述预测时间的变化来修改同时离线床的再生模式操作条件，从而与同时的在线床的同时流模式同时完成了蒸汽床的再生模式。

3. 发明授权

US07413595B2 Control scheme for hybrid PSA/TSA systems 有权
标题翻译：混合PSA / TSA系统的控制方案
公开(公告)号：US07413595B2
公开(公告)日：2008-08-19
申请号：US11101789
申请日：2005-04-08
申请人： William Paul Schmidt , Daniel Patrick Zwilling , Andrew David Wright , Mohammad Ali Kalbassi , Christopher James Raiswell
发明人： William Paul Schmidt , Daniel Patrick Zwilling , Andrew David Wright , Mohammad Ali Kalbassi , Christopher James Raiswell
IPC分类号： B01D53/047 , B01D53/26 , B01J20/34
CPC分类号： B01D53/0462 , B01D53/0431 , B01D53/047 , B01D53/261 , B01D2253/104 , B01D2253/106 , B01D2253/108 , B01D2257/504 , B01D2257/80 , B01D2259/40007 , B01D2259/4009 , B01D2259/4145 , B01D2259/416 , B01J20/08 , B01J20/103 , B01J20/18 , B01J20/3408 , B01J20/3433 , B01J20/3483 , B01J20/3491 , Y02C10/08
摘要： An improved control scheme is set forth for an adsorption process that removes water and carbon dioxide (CO2) from a feed gas using a hybrid of both temperature swing (i.e. TSA) and pressure swing (PSA) to regenerate the adsorbent. The control scheme comprises adjusting the quantity of heat to be provided by the regeneration gas as a function of temperature data taken within a strategic portion of the water selective adsorbent zone. The strategic portion corresponds to the location for the desired transition from regeneration by temperature swing, to regeneration by pressure swing. In a preferred embodiment of the present invention, said quantity of regeneration heat is also adjusted as a function of the water content of the feed gas.
摘要翻译：阐述了一种改进的控制方案，用于使用两种温度摆动（即TSA）和压力摆动（PSA）的混合物从进料气体中除去水和二氧化碳（CO 2 H 2）至吸附过程，再生吸附剂。控制方案包括根据在水选择性吸附剂区域的战略部分中获取的温度数据来调节由再生气体提供的热量。战略部分对应于通过温度摆动从再生到通过压力摆动再生的期望过渡的位置。在本发明的优选实施方案中，所述再生热量也作为进料气体的水含量的函数被调节。

4. 发明申请

US20120009109A1 Treatment of Flue Gas From an Oxyfuel Combustion Process 有权
标题翻译：从燃油燃烧过程中处理烟气
公开(公告)号：US20120009109A1
公开(公告)日：2012-01-12
申请号：US12832156
申请日：2010-07-08
申请人： Andrew David Wright , Vincent White , Timothy Christopher Golden
发明人： Andrew David Wright , Vincent White , Timothy Christopher Golden
IPC分类号： B01D53/62 , B01D53/56 , B01J8/00 , C01B31/20
CPC分类号： B01D53/75 , B01D53/002 , B01D53/0462 , B01D53/047 , B01D53/1456 , B01D53/229 , B01D53/864 , B01D53/8646 , B01D2255/2073 , B01D2255/20761 , B01D2256/22 , B01D2257/302 , B01D2257/404 , B01D2257/502 , B01D2257/80 , B01D2258/0283 , F23G7/07 , F23J2215/40 , F23J2215/50 , F25J3/067 , F25J2205/40 , F25J2205/66 , F25J2205/80 , F25J2205/82 , F25J2210/70 , F25J2220/02 , F25J2220/04 , F25J2220/82 , F25J2220/84 , F25J2230/30 , F25J2230/32 , F25J2230/80 , F25J2240/90 , Y02C10/12 , Y02E20/12 , Y02E20/344
摘要： Carbon monoxide (CO) may be removed from flue gas generated by oxyfuel combustion of a hydrocarbon or carbonaceous fuel, by contacting the flue gas, or a CO-containing gas derived therefrom, at a first elevated temperature, e.g. at least 80° C., and at a first elevated pressure, e.g. at least 2 bar (0.2 MPa), with at least one catalyst bed comprising a CO-oxidation catalyst in the presence of oxygen (O2) to convert CO to carbon dioxide and produce carbon dioxide-enriched gas. The carbon dioxide produced from the CO may be recovered from the carbon dioxide-enriched gas using conventional carbon dioxide recovery techniques. NO in the flue gas may also be oxidized to nitrogen dioxide (NO2) and removed using conventional NO2 removal techniques, or may be reduced in the presence of a reducing gas to nitrogen (N2) which does not have to be removed from the gas.
摘要翻译：一氧化碳（CO）可以通过烃或碳质燃料的氧燃料燃烧产生的烟道气中除去，通过在第一升高的温度例如，通过使烟道气或其衍生的含CO气体接触。至少80℃，并且在第一高压下，例如，至少2巴（0.2MPa），其中至少一个催化剂床在氧气（O 2）存在下包含CO氧化催化剂，以将CO转化为二氧化碳并产生富含二氧化碳的气体。可以使用常规的二氧化碳回收技术从CO生成的二氧化碳从富含二氧化碳的气体中回收。废气中的NO也可以被氧化成二氧化氮（NO 2）并且使用常规的NO 2去除技术去除，或者可以在还原气体存在下将氮气（N 2）还原，而不需要从气体中除去。

5. 发明授权

US08012446B1 Recycle TSA regen gas to boiler for oxyfuel operations 有权
标题翻译：回收TSA再生气到锅炉进行氧燃料运行
公开(公告)号：US08012446B1
公开(公告)日：2011-09-06
申请号：US12832117
申请日：2010-07-08
申请人： Andrew David Wright , Kevin Boyle Fogash , Vincent White , Jeffrey William Kloosterman , Timothy Christopher Golden , Paul Higginbotham
发明人： Andrew David Wright , Kevin Boyle Fogash , Vincent White , Jeffrey William Kloosterman , Timothy Christopher Golden , Paul Higginbotham
IPC分类号： C01B31/20
CPC分类号： B01D53/02 , B01D53/002 , B01D53/0462 , B01D53/229 , B01D53/75 , B01D53/8625 , B01D53/8646 , B01D2253/102 , B01D2253/104 , B01D2253/106 , B01D2253/108 , B01D2253/1124 , B01D2255/20723 , B01D2255/2073 , B01D2255/20761 , B01D2255/20776 , B01D2256/22 , B01D2257/302 , B01D2257/404 , B01D2257/502 , B01D2257/80 , B01D2258/0283 , B01D2259/40054 , B01D2259/4145 , B01J20/043 , B01J20/06 , B01J20/08 , B01J20/103 , B01J20/18 , B01J20/28052 , B01J20/3408 , B01J20/3433 , B01J20/3483 , B01J20/3491 , B01J23/22 , B01J23/30 , B01J23/34 , B01J23/72 , B01J2220/56 , B01J2220/603 , F23J15/02 , F23J2215/10 , F23J2215/101 , F23J2215/20 , F23J2215/50 , F23J2219/60 , F25J3/067 , F25J2205/40 , F25J2205/66 , F25J2205/80 , F25J2210/70 , F25J2220/82 , F25J2220/84 , F25J2230/30 , F25J2230/32 , F25J2230/80 , F25J2240/90 , Y02A50/2345 , Y02C10/12 , Y02E20/344
摘要： NO2 may be removed from a carbon dioxide feed gas comprising NOx and at least one “non-condensable” gas as contaminants by passing the feed gas at a first elevated pressure through a first adsorption system that selectively adsorbs at least NO2 to produce at least substantially NO2-free carbon dioxide gas. The adsorption system is at least partially regenerated using a carbon dioxide-rich gas recovered from the substantially NO2-free carbon dioxide gas after purification. The invention has particular application in removing NOx and water from flue gas generated by oxyfuel combustion.
摘要翻译： NO 2可以从包含NO x的二氧化碳进料气体和作为污染物的至少一种“不可冷凝”气体中除去，这是通过使进料气体在第一升高的压力下通过选择性吸附至少NO 2的第一吸附系统而产生的，无NO2的二氧化碳气体。在纯化后，使用从基本上不含NO 2的二氧化碳气体回收的富含二氧化碳的气体，吸附系统至少部分再生。本发明特别适用于通过氧燃料燃烧产生的烟气中除去NOx和水。

6. 发明授权

US08752390B2 Method and apparatus for producing power and hydrogen 有权
标题翻译：用于生产电力和氢气的方法和装置
公开(公告)号：US08752390B2
公开(公告)日：2014-06-17
申请号：US12835084
申请日：2010-07-13
申请人： Andrew David Wright , Jeffrey Raymond Hufton , Vincent White , Timothy Christopher Golden
发明人： Andrew David Wright , Jeffrey Raymond Hufton , Vincent White , Timothy Christopher Golden
IPC分类号： F02C6/18 , F02C3/28 , B01D59/26 , B01D53/047
CPC分类号： C01B3/56 , C01B2203/043 , C01B2203/0475 , C01B2203/048 , C01B2203/0485 , Y02C10/08 , Y02E20/16 , Y02E20/18 , Y02P20/129 , Y02P20/13
摘要： Both power and H2 are produced from a gaseous mixture, comprising H2 and CO2, using first and second pressure swing adsorption (PSA) systems in series. The gaseous mixture is fed at super-atmospheric pressure to the first PSA system, which comprises adsorbent that selectively adsorbs CO2 at said pressure, and CO2 is adsorbed, thereby providing an H2-enriched mixture at super-atmospheric pressure. A fuel stream is formed from a portion of the H2-enriched mixture, which is combusted and the combustion effluent expanded to generate power. Another portion of the H2-enriched mixture is sent to the second PSA system, which comprises adsorbent that selectively adsorbs CO2 at super-atmospheric pressure, and CO2 is adsorbed, thereby providing a high purity H2 product. In preferred embodiments, the division of H2-enriched mixture between forming the fuel stream and being fed to the second PSA system is adjustable.
摘要翻译：功率和H2均由使用第一和第二变压吸附（PSA）系统的气态混合物（包括H 2和CO 2）产生。气体混合物在超大气压下进料到第一PSA系统，其包括在所述压力下选择性吸附CO 2的吸附剂，并且CO 2被吸附，从而在超大气压下提供富含H2的混合物。燃料流由富含H2的混合物的一部分形成，其被燃烧并且燃烧流出物膨胀以产生动力。将另一部分富H2混合物送至第二PSA系统，其包括在超大气压下选择性吸附CO 2的吸附剂，并且吸收CO 2，从而提供高纯度H 2产物。在优选的实施方案中，形成燃料流并且被供给到第二PSA系统之间的富氢混合物的分配是可调节的。

7. 发明申请

US20120011856A1 Method and Apparatus for Producing Power and Hydrogen 有权
标题翻译：用于生产电力和氢气的方法和装置
公开(公告)号：US20120011856A1
公开(公告)日：2012-01-19
申请号：US12835084
申请日：2010-07-13
申请人： Andrew David Wright , Jeffrey Raymond Hufton , Vincent White , Timothy Christopher Golden
发明人： Andrew David Wright , Jeffrey Raymond Hufton , Vincent White , Timothy Christopher Golden
IPC分类号： F02C6/18
CPC分类号： C01B3/56 , C01B2203/043 , C01B2203/0475 , C01B2203/048 , C01B2203/0485 , Y02C10/08 , Y02E20/16 , Y02E20/18 , Y02P20/129 , Y02P20/13
摘要： Both power and H2 are produced from a gaseous mixture, comprising H2 and CO2, using first and second pressure swing adsorption (PSA) systems in series. The gaseous mixture is fed at super-atmospheric pressure to the first PSA system, which comprises adsorbent that selectively adsorbs CO2 at said pressure, and CO2 is adsorbed, thereby providing an H2-enriched mixture at super-atmospheric pressure. A fuel stream is formed from a portion of the H2-enriched mixture, which is combusted and the combustion effluent expanded to generate power. Another portion of the H2-enriched mixture is sent to the second PSA system, which comprises adsorbent that selectively adsorbs CO2 at super-atmospheric pressure, and CO2 is adsorbed, thereby providing a high purity H2 product. In preferred embodiments, the division of H2-enriched mixture between forming the fuel stream and being fed to the second PSA system is adjustable.
摘要翻译：功率和H2均由使用第一和第二变压吸附（PSA）系统的气态混合物（包括H 2和CO 2）产生。气体混合物在超大气压下进料到第一PSA系统，其包括在所述压力下选择性吸附CO 2的吸附剂，并且CO 2被吸附，从而在超大气压下提供富含H2的混合物。燃料流由富含H2的混合物的一部分形成，其被燃烧并且燃烧流出物膨胀以产生动力。将另一部分富H2混合物送至第二PSA系统，其包括在超大气压下选择性吸附CO 2的吸附剂，并且吸收CO 2，从而提供高纯度H 2产物。在优选的实施方案中，形成燃料流并且被供给到第二PSA系统之间的富氢混合物的分配是可调节的。

8. 发明授权

US08323602B2 Treatment of flue gas from an oxyfuel combustion process 有权
标题翻译：处理来自氧燃料燃烧过程的烟道气
公开(公告)号：US08323602B2
公开(公告)日：2012-12-04
申请号：US12832156
申请日：2010-07-08
申请人： Andrew David Wright , Vincent White , Timothy Christopher Golden
发明人： Andrew David Wright , Vincent White , Timothy Christopher Golden
IPC分类号： B01D53/14 , B01D53/56 , C01B31/00 , D01F9/12 , C01D3/00
CPC分类号： B01D53/75 , B01D53/002 , B01D53/0462 , B01D53/047 , B01D53/1456 , B01D53/229 , B01D53/864 , B01D53/8646 , B01D2255/2073 , B01D2255/20761 , B01D2256/22 , B01D2257/302 , B01D2257/404 , B01D2257/502 , B01D2257/80 , B01D2258/0283 , F23G7/07 , F23J2215/40 , F23J2215/50 , F25J3/067 , F25J2205/40 , F25J2205/66 , F25J2205/80 , F25J2205/82 , F25J2210/70 , F25J2220/02 , F25J2220/04 , F25J2220/82 , F25J2220/84 , F25J2230/30 , F25J2230/32 , F25J2230/80 , F25J2240/90 , Y02C10/12 , Y02E20/12 , Y02E20/344
摘要： Carbon monoxide (CO) may be removed from flue gas generated by oxyfuel combustion of a hydrocarbon or carbonaceous fuel, by contacting the flue gas, or a CO-containing gas derived therefrom, at a first elevated temperature, e.g. at least 80° C., and at a first elevated pressure, e.g. at least 2 bar (0.2 MPa), with at least one catalyst bed comprising a CO-oxidation catalyst in the presence of oxygen (O2) to convert CO to carbon dioxide and produce carbon dioxide-enriched gas. The carbon dioxide produced from the CO may be recovered from the carbon dioxide-enriched gas using conventional carbon dioxide recovery techniques. NO in the flue gas may also be oxidized to nitrogen dioxide (NO2) and removed using conventional NO2 removal techniques, or may be reduced in the presence of a reducing gas to nitrogen (N2) which does not have to be removed from the gas.
摘要翻译：一氧化碳（CO）可以通过烃或碳质燃料的氧燃料燃烧产生的烟道气中除去，通过在第一升高的温度例如，通过使烟道气或其衍生的含CO气体接触。至少80℃，并且在第一高压下，例如，至少2巴（0.2MPa），其中至少一个催化剂床在氧气（O 2）存在下包含CO氧化催化剂，以将CO转化为二氧化碳并产生富含二氧化碳的气体。可以使用常规的二氧化碳回收技术从CO生成的二氧化碳从富含二氧化碳的气体中回收。废气中的NO也可以被氧化成二氧化氮（NO 2）并且使用常规的NO 2去除技术去除，或者可以在还原气体存在下将氮气（N 2）还原，而不需要从气体中除去。

9. 发明申请

US20090173752A1 Dispensing Apparatus 审中-公开
标题翻译：点胶装置
公开(公告)号：US20090173752A1
公开(公告)日：2009-07-09
申请号：US10595214
申请日：2004-09-06
申请人： Andrew David Wright
发明人： Andrew David Wright
IPC分类号： B65D88/54
CPC分类号： B05B11/307 , B05B11/3025 , B05B11/304
摘要： A hand-held multi-dose dispensing apparatus (10) comprising a metering chamber (20) having an axis (21), an end portion (22) at one axial end of the chamber (20) and a side body portion (23) extending from the axial end portion (22), a piston arrangement (30) movable with a piston stroke along the axis of the metering chamber (20) with a seal portion (34) of the piston arrangement (30) being slidably engageable with an inside surface of a side portion (23) of the metering chamber, an inlet (27) for fluid to enter the metering chamber (20), and an outlet (31, 32) for fluid to be dispensed from the metering chamber (20), wherein the inlet (27) is provided on the side body portion (23) of the metering chamber and, in use, during a first portion of the piston stroke, the inlet (27) is in fluid communication with the metering chamber (20) and during a second portion of the piston stroke, the seal portion (34) of the piston arrangement (30) blocks the inlet (27) preventing fluid from passing from the inlet (27) into the metering chamber (20). This dispensing apparatus (10) reduces variations in the shot weight dispensed, by the metering of the fluid commencing at the point at which the piston enters the second portion of its stroke blocking off the inlet.
摘要翻译：一种手持式多剂量分配装置（10），包括具有轴线（21）的计量室（20），在所述腔室（20）的一个轴向端部处的端部部分（22）和侧体部分（23）从所述轴向端部（22）延伸的活塞装置（30）可用活塞冲程沿所述计量腔（20）的轴线移动，所述活塞装置（30）的密封部分（34）可滑动地与所述活塞装置用于流体进入计量室（20）的入口（27）和用于从计量室（20）分配的流体的出口（31,32）的出口（31,32），其中入口（27）设置在计量室的侧体部分（23）上，并且在使用中，在活塞冲程的第一部分期间，入口（27）与计量室（20）流体连通）并且在活塞行程的第二部分期间，活塞装置（30）的密封部分（34）阻挡入口（27），以防止流体通过从入口（27）进入计量室（20）。这种分配装置（10）通过从活塞进入其行程的第二部分的点开始计量流体来减少分配的喷射重量的变化，阻止入口。

10. 发明授权

US08268044B2 Separation of a sour syngas stream 有权
标题翻译：分离酸性合成气流
公开(公告)号：US08268044B2
公开(公告)日：2012-09-18
申请号：US12835112
申请日：2010-07-13
申请人： Andrew David Wright , Vincent White , Kevin Boyle Fogash , Jeffrey William Kloosterman , Jeffrey Raymond Hufton , Charles Linford Schaffer
发明人： Andrew David Wright , Vincent White , Kevin Boyle Fogash , Jeffrey William Kloosterman , Jeffrey Raymond Hufton , Charles Linford Schaffer
IPC分类号： B01D53/02
CPC分类号： B01D53/047 , B01D53/229 , B01D2256/16 , B01D2256/20 , B01D2256/22 , B01D2257/304 , B01D2257/504 , B01D2259/40052 , B01D2259/40069 , B01D2259/4065 , Y02C10/08
摘要： A feed stream, comprising hydrogen sulphide (H2S), carbon dioxide (CO2), hydrogen (H2) and, optionally, carbon monoxide (CO), is separated into at least a CO2 product stream and an H2 or H2 and CO product stream. The stream is separated using a pressure swing adsorption system, an H2S removal system and a further separation system, which systems are used in series to separate the stream. The method has particular application in the separation of a sour (i.e. sulphur containing) syngas, as for example produced from the gasification of solid or heavy liquid carbonaceous feedstock.
摘要翻译：将包含硫化氢（H 2 S），二氧化碳（CO 2），氢气（H 2）和任选的一氧化碳（CO））的进料流分离成至少二氧化碳产物流和H 2或H 2和CO产物流。使用变压吸附系统，H 2 S去除系统和另外的分离系统分离流，该系统串联使用以分离流。该方法特别适用于分离酸（即含硫）合成气，例如由固体或重质液体碳质原料的气化产生。

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