CN102985665A - 低排放三循环动力产生系统和方法 - Google Patents
低排放三循环动力产生系统和方法 Download PDFInfo
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Abstract
提供了用于联合循环动力工厂中的低排放动力产生的方法和系统。一个系统包含燃气涡轮系统,其在压缩的再循环流的存在下化学计量地燃烧燃料和氧化剂,以提供机械动力和气态废气。压缩的再循环流用作稀释剂以调节燃烧工艺的温度。增压器可在气态废气被压缩成为压缩的再循环流之前提高气态废气的压力。净化流从压缩的再循环流流出并且被引导至排出CO2和富氮气体的CO2分离器,CO2和富氮气体可在气体膨胀器中膨胀以产生额外的机械动力。
Description
相关申请的交叉引用
本申请要求于2010年7月2日提交的,名称为“Low EmissionTriple-Cycle Power Generation Systems and Methods(低排放三循环动力产生系统和方法)”的美国临时专利申请61/361,173的权益,其在此通过引用全文并入。
本申请含有涉及以下的主题:于2010年7月2日提交的,名称为“Systems and Methods for Controlling Combustion of a Fuel(控制燃料燃烧的系统和方法)”的美国专利申请号61/361,169;于2010年7月2日提交的,名称为“Low Emission Triple-Cycle Power Generation Systems andMethods(低排放三循环动力产生系统和方法)”的美国专利申请号61/361,170;于2010年7月2日提交的,名称为“Stoichiometric CombustionWith Exhaust Gas Recirculation and Direct Contact Cooler(具有废气再循环和直接接触冷却器的化学计量的燃烧)”的美国专利申请号61/361,176;于2010年7月2日提交的,名称为“Stoichiometric Combustion ofEnriched AirWith Exhaust Gas Recirculation(具有废气再循环的富集空气的化学计量的燃烧)”的美国专利申请号61/361,178,和于2010年7月2日提交的,名称为“Low Emission Power Generation Systems and Methods(低排放动力产生系统和方法)”的美国专利申请号61/361,180。
技术领域
本公开的实施方式涉及联合循环动力系统中的低排放动力产生。更具体地,本公开的实施方式涉及为了增强的CO2制造和捕获以及富氮气体的膨胀或压缩,化学计量地燃烧燃料的方法和装置。
背景技术
本章节意欲介绍本领域的多个方面,其可与本公开的示例性实施方式相关。相信该讨论帮助提供框架,以便于更好地理解本公开的具体方面。因此,应当理解应据此阅读本章节,并不必承认为现有技术。
很多产油国家正经历动力需求的强烈国内增长并对提高采收率法采油(EOR)感兴趣,以提高从他们油藏采油。两种常见的EOR技术包含用于油藏压力保持的氮气(N2)注入和用于EOR的混相驱动(miscible flooding)的二氧化碳(CO2)注入。也存在关于温室气体(GHG)排放的全球关注。该关注连同很多国家中的限制和交易政策的执行使得减少CO2排放成为这些和其他国家以及其中操作烃生产系统的公司优先考虑的事。
一些降低CO2排放的方法包含燃料去碳化或利用溶剂诸如胺类的燃烧后捕获。然而,这两种方案昂贵并降低动力产生效力,导致较低的动力产生、增加的燃料需求和增加的电成本以满足国内动力需求。具体地,氧、SOX和NOX成分的存在使得胺溶剂吸收的使用非常成问题。另一种方法是在结合循环中的含氧燃料(oxyfuel)燃气涡轮(例如,其中来自燃气涡轮布雷顿循环的废热被捕获以制造蒸汽并且在兰金循环中产生额外的动力)。然而,没有可在这样的循环中运转的商业可得的燃气涡轮,并且生产高纯氧要求的动力显著降低了该工艺的总体效力。一些研究已经比较了这些工艺并显示每种方法的一些优势。见例如BOLLAND,OLAV,和UNDRUM,HENRIETTE,Removal of CO2 from Gas Turbine Power Plants:Evaluation ofpre-and post-combustion methods,SINTEF Group,found athttp://www.energy.sintef.no/publ/xergi/98/3/3art-8-engelsk.htm(1998)。
降低CO2排放的其他方法包含诸如在天然气联合循环(NGCC)中的化学计量的废气再循环。在常规NGCC系统中,仅要求大约40%的空气吸入体积,以提供燃料的充分的化学计量的燃烧,而剩余60%的空气体积用于调节温度和冷却烟道气,以便适于引入随后的膨胀器,但也不利地产生难以去除的过量的氧副产品。典型的NGCC产生低压烟道气,其要求一部分产生的动力提取CO2,用于埋存(sequestration)或EOR,由此减少NGCC的热效力。进一步,用于CO2提取的设备大并且昂贵,而且需要数个压缩阶段以便使环境压力气体达到EOR或埋存所需的压力。这样的限制是来自与其他化石燃料诸如煤的燃烧相关的低压烟道气的燃烧后碳捕获的典型特征。
因此,仍然存在对低排放、高效力动力产生和CO2捕获或制造工艺的实质需要。
发明内容
本公开涉及操作系统的三循环动力产生系统和方法。在一个示例性系统中,综合系统包括燃气涡轮系统、废气再循环系统和气体膨胀器。燃气涡轮系统具有第一燃烧室,其被配置用于在压缩的再循环流的存在下化学计量地燃烧第一压缩的氧化剂和第一燃料。燃烧室引导第一排出物流至膨胀器,以产生气态废流和至少部分地驱动主压缩机。废气再循环系统接收来自燃气涡轮系统的膨胀器的气态废流并从其中含有的热能产生动力,诸如通过热回收蒸汽产生单元。废气再循环系统进一步按路线发送废气流至主压缩机,在那里将其压缩以产生压缩的再循环流。压缩的再循环流被引导至燃烧室以用作稀释剂,其被配置用于调节第一排出物流的温度。综合系统进一步包含经净化流流体连接至压缩的再循环流的CO2分离器。CO2分离器从净化流产生富含CO2流和残余流,包括富氮气体。如以上指示的,综合系统也包含气体膨胀器。气体膨胀器经残余流被流体连接至CO2分离器,因为其适于通过使残余流膨胀产生动力。
在操作三循环动力产生系统的示例性方法中,产生动力的方法可包括在第一燃烧室中和在压缩的再循环流的存在下,化学计量地燃烧第一压缩的氧化剂和第一燃料。燃烧可从而产生第一排出物流。压缩的再循环流可用作稀释剂,其被配置用于调节第一排出物流的温度。该方法进一步包含在膨胀器中使第一排出物流膨胀以至少部分地驱动第一压缩机并产生气态废流。第一排出物流的膨胀可产生额外的动力用于其他用途。该方法进一步包含引导气态废流进入第一压缩机,其中第一压缩机压缩气态废流并从而产生压缩的再循环流。仍然进一步地,该方法包含经净化流提取一部分压缩的再循环流至CO2分离器,CO2分离器经源于CO2分离器并主要由富氮气体组成的残余流流体连接至气体膨胀器。示例性方法进一步包含在气体膨胀器中使残余流膨胀,以产生机械动力和废气。
附图说明
本公开的上述和其他优势可在回顾以下详细描述和实施方式的非限制性实施例的附图后变得显而易见,其中:
图1描绘了根据本公开的一种或多种实施方式的用于低排放动力产生和增强的CO2回收的综合系统。
图2描绘了根据本公开的一种或多种实施方式的用于低排放动力产生和增强的CO2回收的另一个综合系统。
图3描绘了根据本公开的一种或多种实施方式的用于低排放动力产生和增强的CO2回收的另一个综合系统。
图4描绘了根据本公开的一种或多种实施方式的用于低排放动力产生和增强的CO2回收的另一个综合系统。
图5描绘了根据本公开的一种或多种实施方式的用于低排放动力产生和增强的CO2回收的另一个综合系统。
图6描绘了根据本公开的一种或多种实施方式的用于低排放动力产生和增强的CO2回收的另一个综合系统。
图7描绘了根据本公开的一种或多种实施方式的用于低排放动力产生和增强的CO2回收的另一个综合系统。
图8描绘了根据本公开的一种或多种实施方式的用于低排放动力产生和增强的CO2回收的另一个综合系统。
发明详述
在以下详述部分,本公开的具体实施方式结合优选实施方式进行描述。然而,对于以下描述对于本公开的特定实施方式或特定用途是特异性的而言,意欲仅用于示例性目的和简单地提供示例性实施方式的描述。因此,本公开不限于以下描述的具体实施方式,而是它包含落入所附权利要求的真实精神和范围内的所有可选方案、更改和等价物。
本文所用的多种术语定义如下。对于在权利要求中使用的术语在以下未定义而言,其应该给予在已经给予该术语的相关领域中的人最广泛的定义,如在至少一个印刷出版物或授权的专利中反映的。
如本文所用的,术语“天然气”指的是从原油井(相关的气体)或从地下含气地层(非相关的气体)获得的多成分气体。天然气的组成和压力可显著变化。典型的天然气流含有甲烷(CH4)作为主要成分,即大于50mol%的天然气流为甲烷。天然气流也可含有乙烷(C2H6)、较高分子量烃(例如,C3-C20烃)、一种或多种酸性气体(例如,硫化氢、二氧化碳)或其任何组合。天然气也可含有少量杂质,诸如水、氮气、硫化铁、蜡、原油或其任何组合。
如本文所用的,术语“化学计量的燃烧”指的是具有一定体积的包括燃料和氧化剂的反应物和一定体积的由燃烧反应物形成的产物的燃烧反应,其中反应物的整个体积用于形成该产物。如本文所用的,术语“基本上化学计量的燃烧”指的是具有燃烧燃料与氧的摩尔比在以下范围中的燃烧反应:从大约化学计量比要求的氧加或减10%,或更优选从大约化学计量比要求的氧加或减5%。例如,对于甲烷,燃料与氧的化学计量比为1:2(CH4+2O2>CO2+2H2O)。丙烷将具有燃料与氧为1:5的化学计量比。测量基本上化学计量的燃烧的另一种方法为供应的氧与化学计量的燃烧需要的氧的比,诸如从大约0.9:1至大约1.1:1,或更优选从大约0.95:1至大约1.05:1。
如本文所用的,术语“流”指的是一定体积的流体,尽管使用术语流通常表示移动体积的流体(例如,具有速度或质量流速)。然而,术语“流”不要求速度、质量流速或特定类型的用于封闭流的管道。
目前公开的系统和工艺的实施方式可用于生产超低排放电力和CO2,用于提高采收率法采油(EOR)或埋存应用。根据本文公开的实施方式,空气和燃料的混合物可化学计量地燃烧并且同时与再循环的废气流混合。通常包含燃烧产物诸如CO2的再循环的废气流可用作稀释剂以控制或以其他方式调节化学计量的燃烧和进入随后的膨胀器的烟道气的温度。
在接近化学计量的条件下的燃烧(或“轻微富(slightly rich)”燃烧)可证明是有利的,以便消除过量氧去除的成本。通过冷却烟道气和从流冷凝出水,可以产生相对高含量的CO2流。尽管一部分再循环的废气可用于闭合布雷顿循环中的温度调节,但剩余的净化流可用于EOR应用,并且可产生电力,很少或没有SOX、NOX或CO2排放至大气。例如,根据本文公开的实施方式,净化流可在适于排出富氮气体的CO2分离器中被处理,其可随后在气体膨胀器中膨胀,以产生额外的机械动力。本文公开的系统的结果是在三个分开的循环中产生动力,并以更经济有效的水平制造或捕获额外的CO2。在一些实施中,富氮排出物流可通过多种方式进行加热,以便增加在氮气流上通过膨胀器可获得的动力。另外地,在一些实施中,膨胀器后的氮气出口可被冷却并且用于提供制冷,其可用于改善布雷顿循环中和/或回收废气中的压缩机(一个或多个)的效力。冷氮气流也可用于改善工艺效力的其他应用。
可选地,排出的富氮气体可被发送至EOR设施,用于额外的压缩和/或注入井用于采油和/或压力保持。尽管可能完全独立地生产用于油藏压力保持的氮气和用于EOR的CO2,但本文公开的实施方式利用协同作用,当在综合工艺中生产氮气和CO2两者时,有可能以低得多的成本完成这些气体的生产,同时也产生动力。
现在参考图,图1说明了动力产生系统100,其被配置用于提供利用联合循环布置的改善的燃烧后CO2捕获工艺。在至少一个实施方式中,动力产生系统100可包含燃气涡轮系统102,其可以表征为闭合的布雷顿循环。在一个实施方式中,燃气涡轮系统102可具有通过公共轴108或其他机械、电或其他动力连接连接至膨胀器106的第一或主压缩机104,从而允许由膨胀器106产生的机械能的一部分驱动压缩机104。膨胀器106也可产生用于其他用途的动力。燃气涡轮系统102可为标准燃气涡轮,其中主压缩机104和膨胀器106分别形成标准燃气涡轮的压缩机和膨胀器末端。然而,在其他实施方式中,主压缩机104和膨胀器106可为系统102中单独的组件。
燃气涡轮系统102也可包含燃烧室110,其被配置用于燃烧与压缩的氧化剂114混合的燃料流112。在一种或多种实施方式中,燃料流112可包含任何合适的烃气体或液体,诸如天然气、甲烷、乙烷、石脑油、丁烷、丙烷、合成气、柴油、煤油、航空燃料、煤衍生的燃料、生物燃料、氧化烃原料或其组合。压缩的氧化剂114可源于流体连接至燃烧室110并且适于压缩供应氧化剂120的第二或入口压缩机118。在一种或多种实施方式中,供应氧化剂120可包含任何合适的含氧气体,诸如空气、富氧空气、氧耗尽的空气、纯氧或其组合。
如将在以下更详细地描述的,燃烧室110也可接收压缩的再循环流144——其包含主要具有CO2和氮气成分的烟道气。压缩的再循环流144可源于主压缩机104并适于帮助促进压缩的氧化剂114和燃料112中的化学计量的燃烧,并也增加工作流体中CO2的浓度。在压缩的再循环流144的存在下,引导至膨胀器106的入口的排出物流116可作为燃料流112和压缩的氧化剂114的燃烧产物而产生。在至少一个实施方式中,燃料流112可主要为天然气,从而产生包含体积部分的蒸发的水、CO2、氮气、氧化氮(NOX)和氧化硫(SOX)的排出物116。在一些实施方式中,小部分未燃烧的燃料112或其他化合物也可由于燃烧平衡限制存在于排出物116中。当排出物流116通过膨胀器106膨胀时,它产生机械动力,以驱动主压缩机104、发电机或其他设施,并也产生具有提高的CO2含量的气态废流122。
动力产生系统100也可包含废气再循环(EGR)系统124。尽管在图中说明的EGR系统124合并了多种装置,但说明的构造仅是代表性的,并且可使用任何将废气122再循环回主压缩机的系统。在一种或多种实施方式中,EGR系统124可包含流体连接至蒸汽燃气涡轮128的热回收蒸汽发生器(HRSG)126,或类似设备。在至少一个实施方式中,HRSG 126和蒸汽燃气涡轮128的组合可以表征为闭合的兰金循环。结合燃气涡轮系统102、HRSG126和蒸汽燃气涡轮128可形成联合循环动力产生工厂的一部分,诸如天然气联合循环(NGCC)工厂。气态废流122可被发送至HRSG 126,以产生蒸汽的流130和冷却的废气132。在一些实施方式中,蒸汽130可被发送至蒸汽燃气涡轮128以产生额外的电力。
图1说明了任选地可被并入一些实施中的EGR系统124中的额外的装置。冷却的废气132可被发送至至少一个冷却单元134,其被配置用于降低冷却的废气132的温度并且产生冷却的再循环气流140。在一种或多种实施方式中,冷却单元134可为直接接触冷却器、调温冷却器(trim cooler)、机械制冷单元或其组合。冷却单元134也可被配置用于经水排泄流138去除一部分冷凝水,水排泄流138可在至少一个实施方式中经管线141按路线发送至HRSG 126,以提供用于产生额外的蒸汽130的水源。在一种或多种实施方式中,冷却的再循环气流140可被引导至流体连接至冷却单元134的增压器142(如有需要)。在冷却单元134中,冷却冷却的废气132可减少压缩增压器142中冷却的再循环气流140需要的动力或完全消除对它的需要。
增压器142可被配置用于在冷却的再循环气流140被引入主压缩机104之前增加其压力。与常规风扇或鼓风机系统相反,增压器142增加冷却的再循环气流140的总体密度,从而引导相同体积流量至主压缩机104的增加的质量流速。因为主压缩机104通常是体积-流量限制的,引导更多质量流量通过主压缩机104可导致来自主压缩机104的较高排出压力,从而经过膨胀器106转换成较高的压力比。经过膨胀器106产生的较高压力比可允许较高的入口温度,并且因此增加膨胀器106的动力和效力。这可证明是有利的,因为富含CO2的排出物116通常保持较高的比热容。因此,当并入时,冷却单元134和增压器142每一个可适于优化或改进燃气涡轮系统102的操作。
主压缩机104可被配置用于压缩从EGR系统124诸如从增压器142接收的冷却的再循环气流140至稍高于燃烧室110压力的压力,从而产生压缩的再循环流144。在至少一个实施方式中,净化流146可从压缩的再循环流144流出并随后在CO2分离器148中进行处理以在升高的压力下经管线150捕获CO2。管线150中分离的CO2可用于出售,用于需要二氧化碳的另一个工艺,和/或被压缩和注入陆地油藏,用于提高采收率法采油(EOR)、埋存或另一个目的。
基本上耗尽CO2并且主要由氮气组成的残余流151可源于CO2分离器148。在一种或多种实施方式中,残余流151可在气体膨胀器152诸如流体连接至CO2分离器148的产生动力的氮气膨胀器中进行膨胀。如图1-3所描绘的,气体膨胀器152可通过公共轴154或其他机械、电或其他动力任选地连接连接至入口压缩机118,从而允许由气体膨胀器152产生的一部分动力驱动入口压缩机118。在气体膨胀器152中膨胀后,主要由氮气组成的废气156可被排出至大气或在本领域已知的其他下游应用中实施。例如,膨胀的氮气流可用于蒸发冷却工艺,其被配置用于进一步降低废气温度,如在同时提交的名称为“Stoichiometric Combustion with Exhaust GasRecirculation and Direct Contact Cooler(具有废气再循环和直接接触冷却器的化学计量的燃烧)”的美国专利申请中大体描述的,其内容在此通过引用并入至与本公开一致。在至少一个实施方式中,气体膨胀器152、入口压缩机118和CO2分离器的组合可以表征为开放的布雷顿循环,或系统100的第三动力产生部件。
尽管气体膨胀器152和入口压缩机118的组合或连接可类似于开放的布雷顿循环,但气体膨胀器152——不管从入口压缩机118连接或未连接,均提供系统100的第三动力产生部件。例如,气体膨胀器152可用于向其他应用提供动力,并且不直接连接至化学计量的压缩机118。例如,在由膨胀器152产生的动力和压缩机118的要求之间存在大量失配。在这种情况下,膨胀器152可适于驱动需要较少动力的较小的压缩机(未示出)(或驱动入口压缩机118和一种或多种额外的设施)。
还在其他实施方式中,如将在以下参考图8讨论的,气体膨胀器152可用下游压缩机188取代,其被配置用于压缩残余流151和产生适于注入油藏用于压力保持或EOR应用的压缩的废气190。
如本文所述的EGR系统124可被实施以实现动力产生系统100的工作流体中较高浓度的CO2,从而允许更有效的CO2分离,用于随后的埋存、压力保持或EOR应用。例如,本文公开的实施方式可有效增加烟道气废流中CO2的浓度至大约10vol%或更高。为了实现该目标,燃烧室110可适于化学计量地燃烧燃料112和压缩的氧化剂114的进入混合物。为了调节化学计量燃烧的温度,以满足膨胀器106入口温度和成分冷却要求,源于压缩的再循环流144的一部分废气可被注入燃烧室110作为稀释剂。因此,本公开的实施方式可基本上消除来自工作流体的任何过量的氧,同时增加其CO2组分。如此,气态废流122可具有小于大约3.0vol%的氧,或小于大约1.0vol%的氧,或小于大约0.1vol%的氧,或甚至小于大约0.001vol%的氧。在一些实施中,燃烧室110,或更具体地燃烧室的入口流可优选被控制为亚化学计量的燃烧,以进一步减少气态废流122的氧含量。
现在将讨论系统100的示例性操作的细节。如可被理解的,在任何本文公开的实施方式的不同部件中实现或经历的具体温度和压力可取决于使用的氧化剂的纯度和膨胀器、压缩机、冷却器等的具体制造和/或型号等等这些因素变化。因此,将理解本文描述的特定数据仅是为了说明性目的并且不应当被理解为其唯一的解释。例如,在本文所述的一个实施方式中,入口压缩机118可被配置为提供在大约280psia和大约300psia之间范围的压力下的压缩的氧化剂114的化学计量的压缩机。然而,同样在本文中考虑的是航改式(aeroderivative)燃气涡轮技术,其可产生和消耗高达大约750psia和更多的压力。
主压缩机104可被配置用于再循环和压缩再循环的废气成为稍高于燃烧室110压力的压力下或在燃烧室110压力下的压缩的再循环流144,并且在燃烧室110中使用一部分再循环的废气作为稀释剂。因为燃烧室110中需要的稀释剂的量可取决于用于化学计量的燃烧的氧化剂的纯度或膨胀器106的型号,热电偶环和/或氧传感器(未示出)可与燃烧室和/或膨胀器相关连。例如,热电偶和/或氧传感器可被放置在燃烧室110的出口、在膨胀器106的入口上和/或在膨胀器106的出口上。在操作中,热电偶和传感器可适于确定一种或多种流的组成和/或温度,用于确定要求作为稀释剂以冷却燃烧产物至要求的膨胀器入口温度需要的废气的体积。另外地或可选地,热电偶和传感器可适于确定将被注入燃烧室110的氧化剂的量。因此,响应于由热电偶检测的热要求和由氧传感器检测的氧水平,压缩的再循环流144和/或压缩的氧化剂114的体积质量流可被操纵或控制以符合需求。体积质量流速可通过任何合适的流量控制系统进行控制。
在至少一个实施方式中,可在化学计量的燃烧期间通过燃烧室110经历大约12-13psia的压力降。燃料112和压缩的氧化剂114的燃烧可产生大约2000℉和大约3000℉之间的温度以及范围从250psia至大约300psia的压力。因为增加的质量流和源于压缩的再循环流144的富含CO2的工作流体的较高比热容,可实现通过膨胀器106的较高的压力比,从而允许较高的入口温度和增加的膨胀器106动力。
离开膨胀器106的气态废流122可具有在或接近环境的压力。在至少一个实施方式中,气态废流122可具有大约15.2psia的压力。在通过HRSG126之前,气态废流122的温度可从大约1180℉至大约1250℉的范围内,以产生管线130中的蒸汽和冷却的废气132。冷却的废气132可具有从大约190℉至大约200℉范围内的温度。在一种或多种实施方式中,冷却单元134可降低冷却的废气132的温度,从而产生具有温度在大约32℉和120℉之间的冷却的再循环气流140,主要取决于在具体的位置和在具体季节期间的湿球温度。
根据一种或多种实施方式,增压器142可被配置用于提高冷却的再循环体流140的压力至范围从大约17.1psia至大约21psia的压力。结果,主压缩机104接收和压缩具有较高的密度和增加的质量流的再循环的烟道气工作流体,从而允许充分较高的排出压力,同时保持相同或相似的压力比。在至少一个实施方式中,从主压缩机104排出的压缩的再循环流144的温度可为大约800℉,压力为大约280psia。
下表提供了具有和不具有增压器142增加的益处的基于联合循环燃气涡轮的测试结果和性能评估,如本文所述的。
表1
如应从表1显而易见的,由于压力比增加,包含增压器142的实施方式可使得膨胀器106功率(即,“燃气涡轮膨胀器功率”)增加。尽管主压缩机104的功率需求可增加,但它的增加不只被膨胀器106的功率输出增加抵消,从而导致大约1%lhv(较低的加热值)的总体热动力性能效力改善。
另外,增加增压器142也可增加氮气膨胀器152的功率输出和净化流146管线中CO2净化压力。尽管增压器142可增加氮气膨胀器152的功率输出,但在表1中可见氮气膨胀器152是对具有或不具有增压器的总体系统100的效力的显著的促进因素。
由于较高的CO2分压,净化流146的净化压力的增加可导致CO2分离器148中改善的溶剂处理性能。这种改善可包含但不限于,以用于溶剂提取工艺的减小的设备尺寸形式的总体资金花费的减少。
现在参考图2,其描绘的是图1的动力产生系统100的可选实施方式,实施并且描述为系统200。如此,参考图1可更好地理解图2。类似于图1的系统100,图2的系统200包含连接至废气再循环(EGR)系统124或以其他方式由废气再循环(EGR)系统124支持的燃气涡轮系统102。然而,图2中的EGR系统124可包含如此实施方式,其中增压器142跟随HRSG 126或可以其他方式被流体连接至HRSG 126。如此,冷却的废气132可在冷却单元134中被降温之前在增压器142中进行压缩。因此,冷却单元134可用作适于去除由增压器142产生的压缩热的后冷却器。与先前公开的实施方式一样,水排泄流138可或可不按路线发送至HRSG 126,以产生额外的蒸汽130。
冷却的再循环气流140可随后被引导至主压缩机104,在那里它如上所讨论的被进一步压缩,从而产生压缩的再循环流144。如可理解的,在增压器142中压缩后,冷却冷却单元134中冷却的废气132可减少在随后的主压缩机104中压缩冷却的再循环气流140至预定压力需要的动力的量。
图3描绘了图1的低排放动力产生系统100的另一个实施方式,实施为系统300。如此,参考图1和2可更好地理解图3。分别类似于图1和2描述的系统100、200,系统300包含由EGR系统124支持的或以其他方式连接至EGR系统124的燃气涡轮系统102。然而,图3中的EGR系统124可包含第一冷却单元134和第二冷却单元136,在其间具有流体连接的增压器142。与先前的实施方式一样,每个冷却单元134、136都可为直接接触冷却器、调温冷却器或类似物,如本领域已知的。
在一种或多种实施方式中,从HRSG 126排出的冷却的废气132可被发送至第一冷却单元134,以产生冷凝水排泄流138和冷却的再循环气流140。冷却的再循环气流140可被引导至增压器142,以便提高冷却的再循环气流140的压力,并随后将它引导至第二冷却单元136。第二冷却单元136可用作后冷却器,其适于去除由增压器142产生的压缩热,并且也经水排泄流143去除额外的冷凝水。在一种或多种实施方式中,每个水排泄流138、143可或可不按路线发送至HRSG 126,以产生额外的蒸汽130。
冷却的再循环气流140可随后被引入主压缩机104,以产生稍高于燃烧室110压力或处于燃烧室110压力下的压缩的再循环流144。如可理解的,在第一冷却单元134中冷却冷却的废气132可减少在增压器142中压缩冷却的再循环气流140需要的动力的量。另外,进一步冷却第二冷却单元136中的废气可减少压缩冷却的再循环气流140至随后的主压缩机104中的预定压力需要的动力的量。
现在参考图4,其描绘了低排放动力产生系统400的另一个实施方式,在一些方面类似于图3的系统300。如此,可参考图1和3更好地理解图4的系统400。然而,应当注意到参考图1-3公开的单独的实施方式或其组合可结合图4的系统400进行实施和/或省略,而不脱离本公开的范围。例如,如本文他处描述的,并入EGR系统124的具体设施和设备可变化。
如上所述,从主压缩机104排出的压缩的再循环流144的温度可为大约800℉,并且显示大约280psia的压力。因此,从压缩的再循环流144流出的净化流146可显示相似的温度和压力。应当再一次注意具体的温度和压力将取决于膨胀器、压缩机、冷却器等的具体的制造和型号不可避免的改变。因为压力比在具有燃烧后CO2回收的常规天然气联合循环(NGCC)系统中发现的那些高得多,它促进了在CO2分离器148中使用更少能量-密集气体处理工艺。例如,这种升高的温度和压力,结合由燃烧室110中进行的化学计量的燃烧引起的大量缺氧,可允许使用热碳酸钾溶剂,以从净化流146提取CO2。在其他实施方式中,CO2选择性吸附剂可包含但不限于,单乙醇胺(“MEA”)、二乙醇胺(“DEA”)、三乙醇胺(“TEA”)、碳酸钾、甲基二乙醇胺(“MDEA”)、活性甲基二乙醇胺(“aMDEA”)、二甘醇胺(“DGA”)、二异丙醇胺(“DIPA”)、哌嗪(“PZ”)、其衍生物、其混合物或其任何组合。其他合适的吸附剂和技术可包含但不限于碳酸丙烯酯物理吸附剂溶剂以及其他碳酸烷基酯、2至12个甘醇单元的聚乙二醇的二甲基醚(SelexolTM工艺)、n-甲基-吡咯烷酮、环丁砜和使用气体处理工艺。
在一个实施方式中,CO2分离器148中的气体处理工艺可要求净化流146的温度冷却至大约250℉-300℉。为了实现该目标,净化流146可被引导通过热交换器158,诸如流体连接至残余流151的交叉交换热交换器。在至少一个实施方式中,在CO2分离器148中从净化流146提取CO2可留下处于净化流146的升高的压力或接近该升高的压力和在大约150℉的温度下的富氮残余流151。在一个实施方式中,与冷却净化流146相关的热能可经热交换器158被提取并用于再加热残余流151,从而产生具有大约750℉温度和大约270-280psia压力的加热的氮蒸气160。尽管与净化流146的热交换是加热残余流的一种方式,但其他方法也位于本公开的范围内。例如,在一种或多种实施方式中,可利用HRSG 126进行补充加热流151,以供应热以及产生蒸汽130。其他示例性方法在本文中进行描述并且不应该被认为是加热残余流151的可用方法的穷尽列举。
在一种或多种实施方式中,加热的氮蒸气160可随后通过气体膨胀器152进行膨胀。因此,热交换器158中的交叉交换热可被配置用于捕获源于主压缩机104的大量压缩能量并且使用其以使从气体膨胀器152提取的动力最大化,和任选地为化学计量的入口压缩机118提供动力。在至少一个实施方式中,主要由大气压下的氮气组成的废气156可被无害地排出至大气或在本领域已知的其他下游应用中实施。示例性下游应用,诸如蒸发冷却工艺,在同时提交的名称为“Stoichiometric Combustion with ExhaustGas Recirculation and Direct Contact Cooler(具有废气再循环和直接接触冷却器的化学计量的燃烧)”的美国专利申请中进行描述,如上所述。
在启动系统400期间和在正常运行期间,当气体膨胀器152可能不能供应所有需要的动力以运行入口压缩机118时,至少一个发动机162,诸如电动机,可与气体膨胀器152协同使用。例如,发动机(一个或多个)162可具有适当(sensibly)的大小,以便在系统400的正常操作期间,发动机(一个或多个)162可被配置用于从气体膨胀器152供应不足的动力。另外地或可选地,在操作期间,有些时候气体膨胀器152产生比入口压缩机118需要的更多的能量。在一些实施中,至少一个发动机162可为发动机/发生器系统,其被可选择地配置用于诸如从电网向压缩机提供动力或从由涡轮152产生的动力产生电。
现在参考图5,其描绘的是低排放动力产生系统500的另一个实施方式,在一些方面类似于图4的系统400。如此,图5的整个系统500将不进行详细地描述,但可参考图1、3和4最好地理解。应当注意参考图1-4公开的任何实施方式可单独实施或结合系统500实施,而不脱离本公开的范围。
在一个实施方式中,一旦净化流146从压缩的再循环流144中流出,它的温度可由催化装置164中进行的催化工艺升高。在操作中,催化装置164可被配置用于减少净化流中的氧和/或一氧化碳含量,并将其转化为残余CO2和热。催化装置164可为单独的设备或多个并联、串联、或并联和串联的组合的设备。在一个实施方式中,催化装置164可为仅需要少量动力运行的小设备。一个示例性催化装置164可包含通常用于HRSG以满足排放要求的氧还原催化剂。这样的系统通常不被设计以去除大量氧,但是如果显著量的氧保留在压缩的再循环流144中,则净化流146可在进一步处理或使用——例如,用于提高采收率法采油(EOR)、CO2分离等的压缩和注入——之前被再循环通过催化装置164多于一次。
另外,净化流146中的任何残余烃也可在催化装置164中燃烧。在至少一个实施方式中,净化流146的温度可通过完全催化转化存在于净化流146中的大约1200ppm氧,从大约785℉升高至大约825℉。可用于催化装置164的说明性催化剂可包含但不限于,镍、铂、铑、钌、钯、或其衍生物、其混合物、其任何组合。该热含量增加可被引入热交换器158并且与富氮残余流151交叉交换,从而导致加热的氮蒸气160的较高温度,并且促进气体膨胀器152中更有效和有力的膨胀工艺。
如包含气体膨胀器152的三循环系统的仍进一步增强,在一种或多种实施方式中,水可经管线166被注入加热的氮蒸气160中,以增加气体膨胀器152的质量通过量并因此增加产生的动力。水可被处理为雾化水或蒸汽。在至少一个实施方式中,通过注入雾化水或蒸汽提供的补充的动力可增加动力输出从大约169MW至大约181MW。如可理解的,动力输出将通常取决于气体膨胀器的制造和型号。应当注意到经管线166将雾化水或蒸汽注入加热的氮蒸气160中以便增加通过气体膨胀器152的质量流可在本文公开的任何实施方式中实施,而不脱离本公开的范围。
参考图6,其描绘的是低排放动力产生系统600的另一个实施方式,类似于图5的系统500。如此,整个系统600将不进行详细地描述,但可参考图5最好地理解。在一个实施方式中,系统600可包含在气体膨胀器152之前放置的额外的化学计量的燃烧室168。燃烧室168可被配置用于化学计量地燃烧燃料170和压缩的氧化剂172的组合,更像上述的燃烧室110,以便在升高的温度和压力下产生排出物流174。在一个实施方式中,燃料170和压缩的氧化剂172可来自分别与被供应进入第一燃烧室110的燃料112和压缩的氧化剂114相同的来源。在并入额外的燃烧室168的实施中,热交换器158可通过其他手段冷却净化流,诸如通过加热在系统600或他处中的一种或多种其他流。例如,对净化流的热交换器可向HRSG或重整工艺提供额外的热。
在其他实施方式中,特别是其中期望或要求零CO2排放的实施方式,燃料170可主要由氢组成。在至少一个实施方式中,氢燃料可通过重整HRSG 126或单独的HRSG(未示出)中的甲烷产生。在甲烷的重整和水煤气转换后,氢产物流中的CO2可在吸收塔(未示出)例如在CO2分离器148中去除。氢可随后与燃烧室168内的加热的氮蒸气160流中的一些氮气混合,以制造可接受的燃气涡轮燃料。
从热交换器158排出的或从CO2分离器148排出的加热的氮蒸气160可用作稀释剂,其被配置用于调节燃烧和排出物流174的温度。在至少一个实施方式中,在气体膨胀器中膨胀以产生机械动力之前,离开燃烧室168的排出物流174可具有大约2500℉的温度。如将理解的,气体膨胀器152、燃烧室168和入口压缩机118的组合可以表征为分开的标准燃气涡轮系统,其中入口压缩机118成为压缩机末端,并且气体膨胀器152成为燃气涡轮的膨胀器末端。
在一种或多种实施方式中,废气156可具有大约1100℉的温度。在至少一个实施方式中,废气156可被引导至HRSG 126,以回收热作为蒸汽燃气涡轮128中的动力。在其他实施方式中,废气156可被引导至外部HRSG和蒸汽燃气涡轮(未示出),以产生用于其他应用的动力。在任何情况下,富氮残余流151在通过膨胀器152后可以以本文讨论的任何方式进行处理,诸如经氮排出、经埋存、EOR或压力保持操作等。
现在参考图7,描绘的是低排放动力产生系统700的另一个实施方式,类似于图6的系统600。如此,图7的整个系统700将不进行详细地描述,但可参考图6及其所附说明最好地理解。不利用分开的入口压缩机118和氮气膨胀器152(见图1-6),如图7所描绘的系统700可包含第二燃气涡轮系统702,其具有第二压缩机176和第二膨胀器178。在一种或多种实施方式中,第二压缩机176可接收和压缩第二供应氧化剂180。类似于在以上图1-6中显示和描述的供应氧化剂120,第二供应氧化剂180可包含任何合适的含氧气体,诸如空气、富氧空气或其组合。第二压缩机176可被配置用于压缩第二供应氧化剂180并且产生第二压缩的氧化剂182。如所描绘的,燃烧室110要求的压缩的氧化剂114可从第二压缩的氧化剂182流供应或提取,并起到与以上一般描述的相同的作用。
在操作中,燃烧室168可被配置用于化学计量地燃烧燃料170和第二压缩的氧化剂182的组合,以便产生升高的温度和压力的排出物流174。在一种或多种实施方式中,来自热交换器158的氮蒸气160或来自CO2分离器148的残余流可被用作稀释剂,其被配置用于调节第二燃烧室168中的燃烧温度。在一个实施方式中,燃料170可来自与供应进入第一燃烧室110的燃料112诸如烃燃料相同的来源。在其他期望或要求零CO2排放的实施方式中,燃料170可主要由氢组成,如以上参考图6一般描述的。
如果使用烃燃料,则将自然产生CO2排放。然而,因为使用大体纯的氮气流作为稀释剂,与常规NGCC动力工厂相比,产生的CO2排放将显著地小。例如,在一个实施方式中,与常规NGCC动力工厂的大约400lbs/MWhr相比,由系统700产生的CO2排放将仅为大约80lbs/MWhr。在一种或多种实施方式中,来自第二膨胀器178的废气156可具有大约1100℉的温度。在至少一个实施方式中,废气156可被引导至第二HRSG 184,以回收热作为分开的蒸汽燃气涡轮186中的动力。然而,在可选实施方式中,废气156可被引导至第一HRSG 126,以回收热作为蒸汽燃气涡轮128中的动力。在这里,再次可理解废气156在通过第二HRSG 184后可被排出或以其他方式用于如上所述的烃回收操作(未示出)。
如可理解的,图7的系统700可允许利用商业可得的燃气涡轮,而不是经历昂贵的升级以获得定制的空气压缩机和定制的膨胀器。系统700也可以以更高的效力产生更多的净动力,因为第二膨胀器178的入口温度可达到大约2500℉的温度。
现在参考图8,描绘的是低排放动力产生系统800的另一个实施方式,类似于图3的系统300。如此,图8的整个系统800将不进行详细地描述,但可参考图1和3最好地理解。然而,应当注意到,参考图1-6公开的实施方式可单独实施或结合图8的系统800实施,而不脱离本公开的范围。在示例性实施方式中,源于CO2分离器148的主要由氮气组成的残余流151可被引导至下游压缩机188。下游压缩机188可被配置用于压缩残余流151并产生压缩的废气190,该压缩的废气190具有例如大约3400psi的压力,或另外适于注入油藏用于压力保持应用的压力。
用下游压缩机188压缩残余流151在应用中可证明是有利的,在该应用中甲烷气体通常被重新注入烃井以保持井压。根据本文公开的实施方式,氮气可替代地被注入烃井,并且残余的甲烷气体可被出售或以其他方式用作相关应用中的燃料,诸如为燃料流112,170提供燃料(见图6和7)。
继续参考图5-7,下表基于以下提供了测试结果和性能评估:不具有膨胀循环的系统(例如,图8的系统800),燃烧室168中不具有额外的点火的系统(例如,图5的系统500),和燃烧室168中具有额外的点火的系统(例如,分别地图6和7的系统600,700)。数据反映了甲烷燃料170点火用于燃烧。
表2
如应从表2显而易见的,燃烧室168中具有点火的实施方式可产生显著较高的联合循环功率输出;当与在燃烧室168中不实施点火的实施方式相比时,几乎是两倍的功率输出。另外,与不实施这种点火技术的实施方式相反,总体热动力性能效力对于并入如本文公开的点火的系统显示了大约3.3%lhv(较低的加热值)的大量上升或改善。
尽管本公开可易于多种更改和可选形式,但以上讨论的示例性实施方式已经仅以实施例的方式显示。然而,应当再次理解本公开不意欲限于本文公开的特定实施方式。的确,本公开包含所有落入所附权利要求的真实精神和范围内的可选方案、更改和等价物。
Claims (30)
1.综合系统,包括:
具有第一燃烧室的燃气涡轮系统,所述第一燃烧室被配置用于在压缩的再循环流的存在下化学计量地燃烧第一压缩的氧化剂和第一燃料,其中所述燃烧室引导第一排出物流至膨胀器,以产生气态废流并且至少部分地驱动主压缩机;
废气再循环系统,其中所述主压缩机压缩所述气态废流并且从而产生所述压缩的再循环流,所述压缩的再循环流用作稀释剂,其被配置用于调节所述第一排出物流的温度;
CO2分离器,其经净化流流体连接至所述压缩的再循环流;和
气体膨胀器,其经源于所述CO2分离器的主要由富氮气体组成的残余流流体连接至所述CO2分离器。
2.权利要求1所述的系统,其中所述废气再循环系统进一步包括至少一个增压器,其被配置用于在引导冷却的再循环气体进入所述主压缩机之前接收和提高所述气态废流的压力。
3.权利要求2所述的系统,进一步包括流体连接至所述至少一个增压器的第一冷却单元和第二冷却单元,所述第一冷却单元被配置用于在所述气态废流进入所述至少一个增压器之前接收和冷却所述气态废流,和所述第二冷却单元被配置用于接收来自所述至少一个增压器的所述气态废流并且进一步冷却所述气态废流以产生所述冷却的再循环气体。
4.权利要求1所述的系统,进一步包括加热器构件,其适于加热所述残余流产生加热的氮蒸气流。
5.权利要求4所述的系统,其中所述气体膨胀器被配置用于使所述加热的氮蒸气膨胀并且从而产生机械动力和废气。
6.权利要求5所述的系统,进一步包括由通过所述气体膨胀器产生的所述机械动力驱动的入口压缩机,其中所述入口压缩机被配置用于提供所述第一压缩的氧化剂。
7.权利要求4所述的系统,其中所述加热器构件包括流体连接至所述净化流和所述残余流两者的热交换器,所述热交换器被配置用于降低所述净化流的温度并且同时升高所述残余流的温度。
8.权利要求1所述的系统,进一步包括与所述净化流结合放置的催化装置,所述催化装置被配置用于在所述净化流进入所述加热器构件之前升高所述净化流的温度。
9.权利要求4所述的系统,其中所述加热器构件包括流体连接至所述残余流的第二燃烧室并且被配置用于化学计量地燃烧第二燃料和第二压缩的氧化剂,以产生第二排出物流。
10.权利要求9所述的系统,其中所述气体膨胀器被配置用于使所述第二排出物流膨胀并且从而产生机械动力和废气。
11.权利要求9所述的系统,其中所述第一压缩的氧化剂和第二压缩的氧化剂和所述第一燃料和第二燃料分别来自相同的来源。
12.权利要求9所述的系统,其中所述第二燃料为氢燃料。
13.产生动力的方法,包括:
在第一燃烧室中并在压缩的再循环流的存在下化学计量地燃烧第一压缩的氧化剂和第一燃料,从而产生第一排出物流,其中所述压缩的再循环流用作稀释剂,其被配置用于调节所述第一排出物流的温度;
在膨胀器中使所述第一排出物流膨胀,以至少部分地驱动第一压缩机并且产生气态废流;
引导所述气态废流进入所述第一压缩机,其中所述第一压缩机压缩所述气态废流并且从而产生所述压缩的再循环流;
经净化流提取一部分所述压缩的再循环流至CO2分离器,所述CO2分离器经源于所述CO2分离器并且主要由富氮气体组成的残余流流体连接至气体膨胀器;和
在气体膨胀器中使所述残余流膨胀,从而产生机械动力和废气。
14.权利要求13所述的方法,进一步包括增压器和冷却单元中的至少一个,其适于增加所述气态废流的质量流速,以产生再循环气体。
15.权利要求14所述的方法,包括利用流体连接至至少一个增压器的第一冷却单元冷却所述气态废流,所述第一冷却单元被配置用于在所述气态废流进入所述至少一个增压器之前接收和冷却所述气态废流。
16.权利要求15所述的方法,进一步包括利用流体连接至所述至少一个增压器的第二冷却单元冷却来自所述至少一个增压器的所述气态废流,以产生所述再循环气体。
17.权利要求13所述的方法,进一步包括利用由所述气体膨胀器产生的所述机械动力驱动入口压缩机,所述入口压缩机被配置用于产生所述第一压缩的氧化剂。
18.权利要求13所述的方法,进一步包括加热器构件,其适于升高所述残余流的温度,以产生加热的氮蒸气流。
19.权利要求18所述的方法,其中所述加热器构件包括流体连接至所述净化流和所述残余流两者的热交换器,并且进一步包括利用所述热交换器降低所述净化流的温度和升高所述残余流的温度,从而产生所述加热的氮蒸气流。
20.权利要求19所述的方法,进一步包括通过在催化装置中燃烧氧和剩余的燃料升高所述净化流的温度,所述催化装置在所述热交换器之前被布置在所述净化流内。
21.权利要求13所述的方法,进一步包括将水注入所述加热的氮蒸气流以增加所述气体膨胀器的质量通过量。
22.权利要求18所述的方法,其中所述加热器构件包括第二燃烧室,并进一步包括在流体连接至所述残余流的所述第二燃烧室中化学计量地燃烧第二燃料和第二压缩的氧化剂,所述第二燃烧室被配置用于产生第二排出物流。
23.权利要求22所述的方法,进一步包括利用从所述CO2分离器排出的所述残余流调节所述第二排出物流的温度。
24.权利要求20所述的方法,进一步包括在所述气体膨胀器中使所述第二排出物流膨胀,以产生机械动力从而驱动入口压缩机,所述入口压缩机被配置用于产生所述第一压缩的氧化剂。
25.综合系统,包括:
第一燃气涡轮系统,包括:
第一压缩机,其被配置用于接收和压缩再循环的废气,并且提供第一压缩的再循环流;
第一燃烧室,其被配置用于接收所述第一压缩的再循环流、第一压缩的氧化剂和第一燃料流,所述第一燃烧室适于化学计量地燃烧所述第一燃料流和第一压缩的氧化剂,其中所述第一压缩的再循环流用作稀释剂以调节燃烧温度;和
第一膨胀器,其连接至所述第一压缩机并被配置用于接收来自所述第一燃烧室的第一排出物,并且产生所述再循环的废气并且至少部分地驱动所述第一压缩机;
净化流,其从所述压缩的再循环流获得并且在CO2分离器中被处理,以提供CO2流和残余流,所述残余流基本上包括氮气;和
第二燃气涡轮系统,其经所述净化流流体连接至所述第一燃气涡轮系统,所述第二燃气涡轮系统包括:
第二压缩机,其被配置用于接收和压缩供应氧化剂并且产生第二压缩的氧化剂,所述第一压缩的氧化剂至少部分源于所述第二压缩的氧化剂;
第二燃烧室,其被配置用于接收所述第二压缩的氧化剂、来自所述残余流的氮气和第二燃料流,所述第二燃烧室适于化学计量地燃烧所述第二燃料流和第二压缩的氧化剂,其中所述氮气用作稀释剂以调节燃烧温度;和
第二膨胀器,其连接至所述第二压缩机并且被配置用于接收来自所述第二燃烧室的第二排出物并且产生废气和至少部分地驱动所述第二压缩机。
26.权利要求25所述的系统,其中所述第一燃气涡轮系统进一步包括增压器,其被配置用于在注入所述第一压缩机之前增加所述再循环的废气的压力,以提供所述压缩的再循环流。
27.权利要求26所述的系统,其中所述第二燃料为氢燃料。
28.权利要求26所述的系统,其中所述第二燃气涡轮系统进一步包括热回收蒸汽发生器,其被配置用于接收来自所述第二膨胀器的废气并且为蒸汽燃气涡轮提供蒸汽。
29.综合系统,包括:
具有第一燃烧室的燃气涡轮系统,所述第一燃烧室被配置用于在压缩的再循环流的存在下化学计量地燃烧压缩的氧化剂和燃料,其中所述燃烧室向膨胀器提供排出物流,以便产生气态废流并且至少部分地驱动第一压缩机;
具有至少一个增压器的废气再循环系统,所述至少一个增压器被配置用于在引导冷却的再循环气体进入所述第一压缩机之前接收和提高所述气态废流的压力,其中所述第一压缩机压缩所述冷却的再循环气体并且从而产生所述压缩的再循环流,所述压缩的再循环流用作稀释剂,其被配置用于调节所述排出物流的温度;
CO2分离器,其经净化流流体连接至所述压缩的再循环流;和
下游压缩机,其经源于所述CO2分离器并且主要由富氮气体组成的残余流流体连接至所述CO2分离器。
30.权利要求29所述的系统,其中所述下游压缩机被配置用于压缩所述富氮气体用于压力保持。
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105041506A (zh) * | 2014-06-10 | 2015-11-11 | 摩尔动力(北京)技术股份有限公司 | 内燃闭合循环氢燃料热动力系统 |
CN106979073A (zh) * | 2015-12-15 | 2017-07-25 | 通用电气公司 | 生成蒸汽且提供冷却的燃烧气体的系统 |
CN107849976A (zh) * | 2015-06-15 | 2018-03-27 | 八河流资产有限责任公司 | 用于启动发电设备的系统和方法 |
CN107864660A (zh) * | 2014-12-31 | 2018-03-30 | 埃克森美孚上游研究公司 | 估计具有排气再循环的燃气涡轮的燃烧当量比的系统和方法 |
Families Citing this family (105)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8671658B2 (en) | 2007-10-23 | 2014-03-18 | Ener-Core Power, Inc. | Oxidizing fuel |
CN101981272B (zh) | 2008-03-28 | 2014-06-11 | 埃克森美孚上游研究公司 | 低排放发电和烃采收系统及方法 |
CN104098070B (zh) | 2008-03-28 | 2016-04-13 | 埃克森美孚上游研究公司 | 低排放发电和烃采收系统及方法 |
EA026915B1 (ru) | 2008-10-14 | 2017-05-31 | Эксонмобил Апстрим Рисерч Компани | Способы и системы для регулирования продуктов горения |
US8701413B2 (en) | 2008-12-08 | 2014-04-22 | Ener-Core Power, Inc. | Oxidizing fuel in multiple operating modes |
US8621869B2 (en) * | 2009-05-01 | 2014-01-07 | Ener-Core Power, Inc. | Heating a reaction chamber |
EA025821B1 (ru) | 2009-06-05 | 2017-02-28 | Эксонмобил Апстрим Рисерч Компани | Топочная система и способы ее применения |
EP2290202A1 (en) * | 2009-07-13 | 2011-03-02 | Siemens Aktiengesellschaft | Cogeneration plant and cogeneration method |
MY158169A (en) | 2009-11-12 | 2016-09-15 | Exxonmobil Upstream Res Co | Low emission power generation and hydrocarbon recovery systems and methods |
EP2395205A1 (en) * | 2010-06-10 | 2011-12-14 | Alstom Technology Ltd | Power Plant with CO2 Capture and Compression |
TWI593878B (zh) | 2010-07-02 | 2017-08-01 | 艾克頌美孚上游研究公司 | 用於控制燃料燃燒之系統及方法 |
CN103026031B (zh) * | 2010-07-02 | 2017-02-15 | 埃克森美孚上游研究公司 | 低排放三循环动力产生系统和方法 |
CA2801492C (en) | 2010-07-02 | 2017-09-26 | Exxonmobil Upstream Research Company | Stoichiometric combustion with exhaust gas recirculation and direct contact cooler |
WO2012003077A1 (en) | 2010-07-02 | 2012-01-05 | Exxonmobil Upstream Research Company | Low emission triple-cycle power generation systems and methods |
JP5906555B2 (ja) | 2010-07-02 | 2016-04-20 | エクソンモービル アップストリーム リサーチ カンパニー | 排ガス再循環方式によるリッチエアの化学量論的燃焼 |
AU2011271636B2 (en) | 2010-07-02 | 2016-03-17 | Exxonmobil Upstream Research Company | Low emission power generation systems and methods |
WO2012018458A1 (en) | 2010-08-06 | 2012-02-09 | Exxonmobil Upstream Research Company | System and method for exhaust gas extraction |
CN105736150B (zh) | 2010-08-06 | 2018-03-06 | 埃克森美孚上游研究公司 | 优化化学计量燃烧的系统和方法 |
AU2011316690C1 (en) * | 2010-10-12 | 2017-01-19 | Allergan, Inc. | Cyclosporin analogs |
TWI564474B (zh) | 2011-03-22 | 2017-01-01 | 艾克頌美孚上游研究公司 | 於渦輪系統中控制化學計量燃燒的整合系統和使用彼之產生動力的方法 |
TWI593872B (zh) | 2011-03-22 | 2017-08-01 | 艾克頌美孚上游研究公司 | 整合系統及產生動力之方法 |
TWI563166B (en) | 2011-03-22 | 2016-12-21 | Exxonmobil Upstream Res Co | Integrated generation systems and methods for generating power |
TWI563165B (en) | 2011-03-22 | 2016-12-21 | Exxonmobil Upstream Res Co | Power generation system and method for generating power |
US9273606B2 (en) | 2011-11-04 | 2016-03-01 | Ener-Core Power, Inc. | Controls for multi-combustor turbine |
US9279364B2 (en) | 2011-11-04 | 2016-03-08 | Ener-Core Power, Inc. | Multi-combustor turbine |
CN104428490B (zh) | 2011-12-20 | 2018-06-05 | 埃克森美孚上游研究公司 | 提高的煤层甲烷生产 |
US9206980B2 (en) | 2012-03-09 | 2015-12-08 | Ener-Core Power, Inc. | Gradual oxidation and autoignition temperature controls |
US9381484B2 (en) | 2012-03-09 | 2016-07-05 | Ener-Core Power, Inc. | Gradual oxidation with adiabatic temperature above flameout temperature |
US9273608B2 (en) | 2012-03-09 | 2016-03-01 | Ener-Core Power, Inc. | Gradual oxidation and autoignition temperature controls |
US8807989B2 (en) * | 2012-03-09 | 2014-08-19 | Ener-Core Power, Inc. | Staged gradual oxidation |
US9234660B2 (en) | 2012-03-09 | 2016-01-12 | Ener-Core Power, Inc. | Gradual oxidation with heat transfer |
US9353946B2 (en) | 2012-03-09 | 2016-05-31 | Ener-Core Power, Inc. | Gradual oxidation with heat transfer |
US9534780B2 (en) | 2012-03-09 | 2017-01-03 | Ener-Core Power, Inc. | Hybrid gradual oxidation |
US9371993B2 (en) | 2012-03-09 | 2016-06-21 | Ener-Core Power, Inc. | Gradual oxidation below flameout temperature |
US9726374B2 (en) * | 2012-03-09 | 2017-08-08 | Ener-Core Power, Inc. | Gradual oxidation with flue gas |
US9567903B2 (en) | 2012-03-09 | 2017-02-14 | Ener-Core Power, Inc. | Gradual oxidation with heat transfer |
US9359947B2 (en) | 2012-03-09 | 2016-06-07 | Ener-Core Power, Inc. | Gradual oxidation with heat control |
US9017618B2 (en) | 2012-03-09 | 2015-04-28 | Ener-Core Power, Inc. | Gradual oxidation with heat exchange media |
US8980192B2 (en) | 2012-03-09 | 2015-03-17 | Ener-Core Power, Inc. | Gradual oxidation below flameout temperature |
US9347664B2 (en) | 2012-03-09 | 2016-05-24 | Ener-Core Power, Inc. | Gradual oxidation with heat control |
US9328916B2 (en) | 2012-03-09 | 2016-05-03 | Ener-Core Power, Inc. | Gradual oxidation with heat control |
US9194584B2 (en) | 2012-03-09 | 2015-11-24 | Ener-Core Power, Inc. | Gradual oxidation with gradual oxidizer warmer |
US8980193B2 (en) | 2012-03-09 | 2015-03-17 | Ener-Core Power, Inc. | Gradual oxidation and multiple flow paths |
US9267432B2 (en) | 2012-03-09 | 2016-02-23 | Ener-Core Power, Inc. | Staged gradual oxidation |
US8926917B2 (en) | 2012-03-09 | 2015-01-06 | Ener-Core Power, Inc. | Gradual oxidation with adiabatic temperature above flameout temperature |
US9359948B2 (en) | 2012-03-09 | 2016-06-07 | Ener-Core Power, Inc. | Gradual oxidation with heat control |
US9328660B2 (en) | 2012-03-09 | 2016-05-03 | Ener-Core Power, Inc. | Gradual oxidation and multiple flow paths |
US9353682B2 (en) | 2012-04-12 | 2016-05-31 | General Electric Company | Methods, systems and apparatus relating to combustion turbine power plants with exhaust gas recirculation |
US9784185B2 (en) | 2012-04-26 | 2017-10-10 | General Electric Company | System and method for cooling a gas turbine with an exhaust gas provided by the gas turbine |
US10273880B2 (en) | 2012-04-26 | 2019-04-30 | General Electric Company | System and method of recirculating exhaust gas for use in a plurality of flow paths in a gas turbine engine |
US9708977B2 (en) | 2012-12-28 | 2017-07-18 | General Electric Company | System and method for reheat in gas turbine with exhaust gas recirculation |
US9599070B2 (en) | 2012-11-02 | 2017-03-21 | General Electric Company | System and method for oxidant compression in a stoichiometric exhaust gas recirculation gas turbine system |
US10161312B2 (en) | 2012-11-02 | 2018-12-25 | General Electric Company | System and method for diffusion combustion with fuel-diluent mixing in a stoichiometric exhaust gas recirculation gas turbine system |
US9574496B2 (en) | 2012-12-28 | 2017-02-21 | General Electric Company | System and method for a turbine combustor |
US9631815B2 (en) | 2012-12-28 | 2017-04-25 | General Electric Company | System and method for a turbine combustor |
US9869279B2 (en) | 2012-11-02 | 2018-01-16 | General Electric Company | System and method for a multi-wall turbine combustor |
US10107495B2 (en) | 2012-11-02 | 2018-10-23 | General Electric Company | Gas turbine combustor control system for stoichiometric combustion in the presence of a diluent |
US10215412B2 (en) | 2012-11-02 | 2019-02-26 | General Electric Company | System and method for load control with diffusion combustion in a stoichiometric exhaust gas recirculation gas turbine system |
US9803865B2 (en) | 2012-12-28 | 2017-10-31 | General Electric Company | System and method for a turbine combustor |
US9611756B2 (en) | 2012-11-02 | 2017-04-04 | General Electric Company | System and method for protecting components in a gas turbine engine with exhaust gas recirculation |
US10208677B2 (en) | 2012-12-31 | 2019-02-19 | General Electric Company | Gas turbine load control system |
US9581081B2 (en) | 2013-01-13 | 2017-02-28 | General Electric Company | System and method for protecting components in a gas turbine engine with exhaust gas recirculation |
US9512759B2 (en) | 2013-02-06 | 2016-12-06 | General Electric Company | System and method for catalyst heat utilization for gas turbine with exhaust gas recirculation |
TW201502356A (zh) | 2013-02-21 | 2015-01-16 | Exxonmobil Upstream Res Co | 氣渦輪機排氣中氧之減少 |
US9938861B2 (en) | 2013-02-21 | 2018-04-10 | Exxonmobil Upstream Research Company | Fuel combusting method |
WO2014133406A1 (en) | 2013-02-28 | 2014-09-04 | General Electric Company | System and method for a turbine combustor |
JP6143895B2 (ja) | 2013-03-08 | 2017-06-07 | エクソンモービル アップストリーム リサーチ カンパニー | 発電及びメタンハイドレートからのメタン回収 |
US9618261B2 (en) | 2013-03-08 | 2017-04-11 | Exxonmobil Upstream Research Company | Power generation and LNG production |
US20140250945A1 (en) | 2013-03-08 | 2014-09-11 | Richard A. Huntington | Carbon Dioxide Recovery |
TW201500635A (zh) | 2013-03-08 | 2015-01-01 | Exxonmobil Upstream Res Co | 處理廢氣以供用於提高油回收 |
US9631542B2 (en) | 2013-06-28 | 2017-04-25 | General Electric Company | System and method for exhausting combustion gases from gas turbine engines |
US9835089B2 (en) * | 2013-06-28 | 2017-12-05 | General Electric Company | System and method for a fuel nozzle |
US9617914B2 (en) | 2013-06-28 | 2017-04-11 | General Electric Company | Systems and methods for monitoring gas turbine systems having exhaust gas recirculation |
TWI654368B (zh) | 2013-06-28 | 2019-03-21 | 美商艾克頌美孚上游研究公司 | 用於控制在廢氣再循環氣渦輪機系統中的廢氣流之系統、方法與媒體 |
US9903588B2 (en) | 2013-07-30 | 2018-02-27 | General Electric Company | System and method for barrier in passage of combustor of gas turbine engine with exhaust gas recirculation |
US9587510B2 (en) | 2013-07-30 | 2017-03-07 | General Electric Company | System and method for a gas turbine engine sensor |
US9951658B2 (en) | 2013-07-31 | 2018-04-24 | General Electric Company | System and method for an oxidant heating system |
US9752458B2 (en) | 2013-12-04 | 2017-09-05 | General Electric Company | System and method for a gas turbine engine |
US10030588B2 (en) | 2013-12-04 | 2018-07-24 | General Electric Company | Gas turbine combustor diagnostic system and method |
US10227920B2 (en) | 2014-01-15 | 2019-03-12 | General Electric Company | Gas turbine oxidant separation system |
US9863267B2 (en) | 2014-01-21 | 2018-01-09 | General Electric Company | System and method of control for a gas turbine engine |
US9915200B2 (en) | 2014-01-21 | 2018-03-13 | General Electric Company | System and method for controlling the combustion process in a gas turbine operating with exhaust gas recirculation |
US10079564B2 (en) | 2014-01-27 | 2018-09-18 | General Electric Company | System and method for a stoichiometric exhaust gas recirculation gas turbine system |
US10047633B2 (en) | 2014-05-16 | 2018-08-14 | General Electric Company | Bearing housing |
US10060359B2 (en) | 2014-06-30 | 2018-08-28 | General Electric Company | Method and system for combustion control for gas turbine system with exhaust gas recirculation |
US10655542B2 (en) | 2014-06-30 | 2020-05-19 | General Electric Company | Method and system for startup of gas turbine system drive trains with exhaust gas recirculation |
US9885290B2 (en) | 2014-06-30 | 2018-02-06 | General Electric Company | Erosion suppression system and method in an exhaust gas recirculation gas turbine system |
US9819292B2 (en) | 2014-12-31 | 2017-11-14 | General Electric Company | Systems and methods to respond to grid overfrequency events for a stoichiometric exhaust recirculation gas turbine |
US10788212B2 (en) | 2015-01-12 | 2020-09-29 | General Electric Company | System and method for an oxidant passageway in a gas turbine system with exhaust gas recirculation |
US10094566B2 (en) | 2015-02-04 | 2018-10-09 | General Electric Company | Systems and methods for high volumetric oxidant flow in gas turbine engine with exhaust gas recirculation |
US10316746B2 (en) | 2015-02-04 | 2019-06-11 | General Electric Company | Turbine system with exhaust gas recirculation, separation and extraction |
US10253690B2 (en) | 2015-02-04 | 2019-04-09 | General Electric Company | Turbine system with exhaust gas recirculation, separation and extraction |
US10267270B2 (en) | 2015-02-06 | 2019-04-23 | General Electric Company | Systems and methods for carbon black production with a gas turbine engine having exhaust gas recirculation |
US10145269B2 (en) | 2015-03-04 | 2018-12-04 | General Electric Company | System and method for cooling discharge flow |
US10480792B2 (en) | 2015-03-06 | 2019-11-19 | General Electric Company | Fuel staging in a gas turbine engine |
MY193222A (en) * | 2015-09-01 | 2022-09-26 | 8 Rivers Capital Llc | Systems and methods for power production using nested co2 cycles |
AU2017252755B2 (en) | 2016-04-21 | 2022-06-16 | 8 Rivers Capital, Llc | Systems and methods for oxidation of hydrocarbon gases |
ES2914625T3 (es) * | 2017-12-22 | 2022-06-14 | Darienzo Giovanni | Sistema de cogeneración para una caldera |
WO2021034221A1 (ru) * | 2019-08-22 | 2021-02-25 | Владимир Николаевич КОСТЮКОВ | Газопаровая энергетическая установка по антони циклу |
CN111463806B (zh) * | 2020-04-23 | 2022-04-01 | 中国科学院武汉岩土力学研究所 | 一种电力储能调峰系统 |
US11619155B2 (en) * | 2021-02-03 | 2023-04-04 | The Boeing Company | Metal catalytic converter system for auxiliary power unit and automobile engine exhausts |
US20230288058A1 (en) * | 2022-03-10 | 2023-09-14 | Uop Llc | Processes and apparatuses for burning a hydrogen fuel and a hydrocarbon fuel |
EP4253742A1 (en) * | 2022-03-29 | 2023-10-04 | Raytheon Technologies Corporation | Recuperated engine with supercritical co2 bottoming cycle |
US20230340914A1 (en) * | 2022-04-20 | 2023-10-26 | Richard Alan Callahan | Turbine Powered Electricity Generation |
US12040513B2 (en) | 2022-11-18 | 2024-07-16 | Carbon Ventures, Llc | Enhancing efficiencies of oxy-combustion power cycles |
Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB631547A (en) * | 1946-10-04 | 1949-11-04 | Sulzer Ag | Improvements relating to plants in which solid material is subjected to heating and cooling |
CN1142004A (zh) * | 1994-08-05 | 1997-02-05 | Abb管理有限公司 | 空气蓄积器式涡轮机 |
US20020166323A1 (en) * | 2001-03-23 | 2002-11-14 | America Air Liquide, Inc. | Integrated air separation and power generation process |
US20030221409A1 (en) * | 2002-05-29 | 2003-12-04 | Mcgowan Thomas F. | Pollution reduction fuel efficient combustion turbine |
CN1959085A (zh) * | 2005-07-08 | 2007-05-09 | 通用电气公司 | 二氧化碳分离的发电系统和方法 |
CN1996652A (zh) * | 2006-12-28 | 2007-07-11 | 上海交通大学 | 高温燃料电池混合动力协调控制系统 |
US20080010967A1 (en) * | 2004-08-11 | 2008-01-17 | Timothy Griffin | Method for Generating Energy in an Energy Generating Installation Having a Gas Turbine, and Energy Generating Installation Useful for Carrying Out the Method |
CN101504154A (zh) * | 2008-02-04 | 2009-08-12 | 通用电气公司 | 用于便于组合循环工作流体的改变及其燃烧的方法和系统 |
US20100115960A1 (en) * | 2007-06-19 | 2010-05-13 | Alstom Technology Ltd | Gas Turbine Installation with Flue Gas Recirculation |
WO2010072729A2 (en) * | 2008-12-24 | 2010-07-01 | Alstom Technology Ltd | Power plant with co2 capture |
Family Cites Families (657)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2488911A (en) | 1946-11-09 | 1949-11-22 | Surface Combustion Corp | Combustion apparatus for use with turbines |
GB776269A (en) | 1952-11-08 | 1957-06-05 | Licentia Gmbh | A gas turbine plant |
US2884758A (en) | 1956-09-10 | 1959-05-05 | Bbc Brown Boveri & Cie | Regulating device for burner operating with simultaneous combustion of gaseous and liquid fuel |
US3366373A (en) * | 1965-06-21 | 1968-01-30 | Zink Co John | Apparatus for adding heat to gas turbine exhaust |
US3561895A (en) | 1969-06-02 | 1971-02-09 | Exxon Research Engineering Co | Control of fuel gas combustion properties in inspirating burners |
US3631672A (en) | 1969-08-04 | 1972-01-04 | Gen Electric | Eductor cooled gas turbine casing |
US3643430A (en) | 1970-03-04 | 1972-02-22 | United Aircraft Corp | Smoke reduction combustion chamber |
US3705492A (en) | 1971-01-11 | 1972-12-12 | Gen Motors Corp | Regenerative gas turbine system |
US3841382A (en) | 1973-03-16 | 1974-10-15 | Maloney Crawford Tank | Glycol regenerator using controller gas stripping under vacuum |
US4455614A (en) * | 1973-09-21 | 1984-06-19 | Westinghouse Electric Corp. | Gas turbine and steam turbine combined cycle electric power generating plant having a coordinated and hybridized control system and an improved factory based method for making and testing combined cycle and other power plants and control systems therefor |
US3949548A (en) | 1974-06-13 | 1976-04-13 | Lockwood Jr Hanford N | Gas turbine regeneration system |
GB1490145A (en) | 1974-09-11 | 1977-10-26 | Mtu Muenchen Gmbh | Gas turbine engine |
US4043395A (en) | 1975-03-13 | 1977-08-23 | Continental Oil Company | Method for removing methane from coal |
US4018046A (en) | 1975-07-17 | 1977-04-19 | Avco Corporation | Infrared radiation suppressor for gas turbine engine |
NL7612453A (nl) | 1975-11-24 | 1977-05-26 | Gen Electric | Geintegreerde lichtgasproduktieinstallatie en werkwijze voor de opwekking van elektrische energie. |
US4033712A (en) * | 1976-02-26 | 1977-07-05 | Edmund D. Hollon | Fuel supply systems |
US4077206A (en) | 1976-04-16 | 1978-03-07 | The Boeing Company | Gas turbine mixer apparatus for suppressing engine core noise and engine fan noise |
US4204401A (en) | 1976-07-19 | 1980-05-27 | The Hydragon Corporation | Turbine engine with exhaust gas recirculation |
US4380895A (en) | 1976-09-09 | 1983-04-26 | Rolls-Royce Limited | Combustion chamber for a gas turbine engine having a variable rate diffuser upstream of air inlet means |
US4066214A (en) | 1976-10-14 | 1978-01-03 | The Boeing Company | Gas turbine exhaust nozzle for controlled temperature flow across adjoining airfoils |
US4117671A (en) | 1976-12-30 | 1978-10-03 | The Boeing Company | Noise suppressing exhaust mixer assembly for ducted-fan, turbojet engine |
US4165609A (en) | 1977-03-02 | 1979-08-28 | The Boeing Company | Gas turbine mixer apparatus |
US4092095A (en) | 1977-03-18 | 1978-05-30 | Combustion Unlimited Incorporated | Combustor for waste gases |
US4112676A (en) | 1977-04-05 | 1978-09-12 | Westinghouse Electric Corp. | Hybrid combustor with staged injection of pre-mixed fuel |
US4271664A (en) | 1977-07-21 | 1981-06-09 | Hydragon Corporation | Turbine engine with exhaust gas recirculation |
RO73353A2 (ro) | 1977-08-12 | 1981-09-24 | Institutul De Cercetari Si Proiectari Pentru Petrol Si Gaze,Ro | Procedeu de desulfurare a fluidelor din zacamintele de hidrocarburi extrase prin sonde |
US4101294A (en) | 1977-08-15 | 1978-07-18 | General Electric Company | Production of hot, saturated fuel gas |
US4160640A (en) | 1977-08-30 | 1979-07-10 | Maev Vladimir A | Method of fuel burning in combustion chambers and annular combustion chamber for carrying same into effect |
US4222240A (en) | 1978-02-06 | 1980-09-16 | Castellano Thomas P | Turbocharged engine |
DE2808690C2 (de) | 1978-03-01 | 1983-11-17 | Messerschmitt-Bölkow-Blohm GmbH, 8000 München | Einrichtung zur Erzeugung von Heißdampf für die Gewinnung von Erdöl |
US4236378A (en) | 1978-03-01 | 1980-12-02 | General Electric Company | Sectoral combustor for burning low-BTU fuel gas |
US4498288A (en) | 1978-10-13 | 1985-02-12 | General Electric Company | Fuel injection staged sectoral combustor for burning low-BTU fuel gas |
US4253301A (en) | 1978-10-13 | 1981-03-03 | General Electric Company | Fuel injection staged sectoral combustor for burning low-BTU fuel gas |
US4345426A (en) | 1980-03-27 | 1982-08-24 | Egnell Rolf A | Device for burning fuel with air |
GB2080934B (en) | 1980-07-21 | 1984-02-15 | Hitachi Ltd | Low btu gas burner |
US4352269A (en) | 1980-07-25 | 1982-10-05 | Mechanical Technology Incorporated | Stirling engine combustor |
GB2082259B (en) | 1980-08-15 | 1984-03-07 | Rolls Royce | Exhaust flow mixers and nozzles |
US4442665A (en) | 1980-10-17 | 1984-04-17 | General Electric Company | Coal gasification power generation plant |
US4488865A (en) | 1980-12-22 | 1984-12-18 | Arkansas Patents, Inc. | Pulsing combustion |
US4479484A (en) | 1980-12-22 | 1984-10-30 | Arkansas Patents, Inc. | Pulsing combustion |
US4480985A (en) | 1980-12-22 | 1984-11-06 | Arkansas Patents, Inc. | Pulsing combustion |
US4637792A (en) | 1980-12-22 | 1987-01-20 | Arkansas Patents, Inc. | Pulsing combustion |
US4344486A (en) | 1981-02-27 | 1982-08-17 | Standard Oil Company (Indiana) | Method for enhanced oil recovery |
US4399652A (en) | 1981-03-30 | 1983-08-23 | Curtiss-Wright Corporation | Low BTU gas combustor |
US4414334A (en) | 1981-08-07 | 1983-11-08 | Phillips Petroleum Company | Oxygen scavenging with enzymes |
US4434613A (en) | 1981-09-02 | 1984-03-06 | General Electric Company | Closed cycle gas turbine for gaseous production |
US4445842A (en) | 1981-11-05 | 1984-05-01 | Thermal Systems Engineering, Inc. | Recuperative burner with exhaust gas recirculation means |
GB2117053B (en) | 1982-02-18 | 1985-06-05 | Boc Group Plc | Gas turbines and engines |
US4498289A (en) | 1982-12-27 | 1985-02-12 | Ian Osgerby | Carbon dioxide power cycle |
US4548034A (en) | 1983-05-05 | 1985-10-22 | Rolls-Royce Limited | Bypass gas turbine aeroengines and exhaust mixers therefor |
US4528811A (en) | 1983-06-03 | 1985-07-16 | General Electric Co. | Closed-cycle gas turbine chemical processor |
GB2149456B (en) | 1983-11-08 | 1987-07-29 | Rolls Royce | Exhaust mixing in turbofan aeroengines |
US4561245A (en) | 1983-11-14 | 1985-12-31 | Atlantic Richfield Company | Turbine anti-icing system |
US4602614A (en) | 1983-11-30 | 1986-07-29 | United Stirling, Inc. | Hybrid solar/combustion powered receiver |
SE439057B (sv) | 1984-06-05 | 1985-05-28 | United Stirling Ab & Co | Anordning for forbrenning av ett brensle med syrgas och inblandning av en del av de vid forbrenningen bildade avgaserna |
EP0169431B1 (en) | 1984-07-10 | 1990-04-11 | Hitachi, Ltd. | Gas turbine combustor |
US4606721A (en) | 1984-11-07 | 1986-08-19 | Tifa Limited | Combustion chamber noise suppressor |
US4653278A (en) | 1985-08-23 | 1987-03-31 | General Electric Company | Gas turbine engine carburetor |
US4651712A (en) | 1985-10-11 | 1987-03-24 | Arkansas Patents, Inc. | Pulsing combustion |
NO163612C (no) | 1986-01-23 | 1990-06-27 | Norsk Energi | Fremgangsmaate og anlegg for fremstilling av nitrogen for anvendelse under hoeyt trykk. |
US4858428A (en) | 1986-04-24 | 1989-08-22 | Paul Marius A | Advanced integrated propulsion system with total optimized cycle for gas turbines |
US4753666A (en) | 1986-07-24 | 1988-06-28 | Chevron Research Company | Distillative processing of CO2 and hydrocarbons for enhanced oil recovery |
US4684465A (en) | 1986-10-10 | 1987-08-04 | Combustion Engineering, Inc. | Supercritical fluid chromatograph with pneumatically controlled pump |
US4681678A (en) | 1986-10-10 | 1987-07-21 | Combustion Engineering, Inc. | Sample dilution system for supercritical fluid chromatography |
US4817387A (en) | 1986-10-27 | 1989-04-04 | Hamilton C. Forman, Trustee | Turbocharger/supercharger control device |
US4762543A (en) | 1987-03-19 | 1988-08-09 | Amoco Corporation | Carbon dioxide recovery |
US5084438A (en) | 1988-03-23 | 1992-01-28 | Nec Corporation | Electronic device substrate using silicon semiconductor substrate |
US4883122A (en) | 1988-09-27 | 1989-11-28 | Amoco Corporation | Method of coalbed methane production |
JP2713627B2 (ja) | 1989-03-20 | 1998-02-16 | 株式会社日立製作所 | ガスタービン燃焼器、これを備えているガスタービン設備、及びこの燃焼方法 |
US4946597A (en) | 1989-03-24 | 1990-08-07 | Esso Resources Canada Limited | Low temperature bitumen recovery process |
US4976100A (en) | 1989-06-01 | 1990-12-11 | Westinghouse Electric Corp. | System and method for heat recovery in a combined cycle power plant |
US5135387A (en) | 1989-10-19 | 1992-08-04 | It-Mcgill Environmental Systems, Inc. | Nitrogen oxide control using internally recirculated flue gas |
US5044932A (en) | 1989-10-19 | 1991-09-03 | It-Mcgill Pollution Control Systems, Inc. | Nitrogen oxide control using internally recirculated flue gas |
SE467646B (sv) | 1989-11-20 | 1992-08-24 | Abb Carbon Ab | Saett vid roekgasrening i pfbc-anlaeggning |
US5123248A (en) | 1990-03-28 | 1992-06-23 | General Electric Company | Low emissions combustor |
JP2954972B2 (ja) | 1990-04-18 | 1999-09-27 | 三菱重工業株式会社 | ガス化ガス燃焼ガスタービン発電プラント |
US5271905A (en) | 1990-04-27 | 1993-12-21 | Mobil Oil Corporation | Apparatus for multi-stage fast fluidized bed regeneration of catalyst |
JPH0450433A (ja) | 1990-06-20 | 1992-02-19 | Toyota Motor Corp | 直列2段過給内燃機関の排気ガス再循環装置 |
US5141049A (en) | 1990-08-09 | 1992-08-25 | The Badger Company, Inc. | Treatment of heat exchangers to reduce corrosion and by-product reactions |
US5154596A (en) | 1990-09-07 | 1992-10-13 | John Zink Company, A Division Of Koch Engineering Company, Inc. | Methods and apparatus for burning fuel with low NOx formation |
US5098282A (en) | 1990-09-07 | 1992-03-24 | John Zink Company | Methods and apparatus for burning fuel with low NOx formation |
US5197289A (en) | 1990-11-26 | 1993-03-30 | General Electric Company | Double dome combustor |
US5085274A (en) | 1991-02-11 | 1992-02-04 | Amoco Corporation | Recovery of methane from solid carbonaceous subterranean of formations |
DE4110507C2 (de) | 1991-03-30 | 1994-04-07 | Mtu Muenchen Gmbh | Brenner für Gasturbinentriebwerke mit mindestens einer für die Zufuhr von Verbrennungsluft lastabhängig regulierbaren Dralleinrichtung |
US5073105A (en) | 1991-05-01 | 1991-12-17 | Callidus Technologies Inc. | Low NOx burner assemblies |
US5147111A (en) | 1991-08-02 | 1992-09-15 | Atlantic Richfield Company | Cavity induced stimulation method of coal degasification wells |
US5255506A (en) | 1991-11-25 | 1993-10-26 | General Motors Corporation | Solid fuel combustion system for gas turbine engine |
US5183232A (en) | 1992-01-31 | 1993-02-02 | Gale John A | Interlocking strain relief shelf bracket |
US5195884A (en) | 1992-03-27 | 1993-03-23 | John Zink Company, A Division Of Koch Engineering Company, Inc. | Low NOx formation burner apparatus and methods |
US5238395A (en) | 1992-03-27 | 1993-08-24 | John Zink Company | Low nox gas burner apparatus and methods |
US5634329A (en) | 1992-04-30 | 1997-06-03 | Abb Carbon Ab | Method of maintaining a nominal working temperature of flue gases in a PFBC power plant |
US5332036A (en) | 1992-05-15 | 1994-07-26 | The Boc Group, Inc. | Method of recovery of natural gases from underground coal formations |
US5295350A (en) | 1992-06-26 | 1994-03-22 | Texaco Inc. | Combined power cycle with liquefied natural gas (LNG) and synthesis or fuel gas |
US6289666B1 (en) | 1992-10-27 | 2001-09-18 | Ginter Vast Corporation | High efficiency low pollution hybrid Brayton cycle combustor |
US5355668A (en) | 1993-01-29 | 1994-10-18 | General Electric Company | Catalyst-bearing component of gas turbine engine |
US5628184A (en) | 1993-02-03 | 1997-05-13 | Santos; Rolando R. | Apparatus for reducing the production of NOx in a gas turbine |
US5361586A (en) | 1993-04-15 | 1994-11-08 | Westinghouse Electric Corporation | Gas turbine ultra low NOx combustor |
US5388395A (en) | 1993-04-27 | 1995-02-14 | Air Products And Chemicals, Inc. | Use of nitrogen from an air separation unit as gas turbine air compressor feed refrigerant to improve power output |
US5444971A (en) | 1993-04-28 | 1995-08-29 | Holenberger; Charles R. | Method and apparatus for cooling the inlet air of gas turbine and internal combustion engine prime movers |
US5359847B1 (en) | 1993-06-01 | 1996-04-09 | Westinghouse Electric Corp | Dual fuel ultra-flow nox combustor |
US5638674A (en) | 1993-07-07 | 1997-06-17 | Mowill; R. Jan | Convectively cooled, single stage, fully premixed controllable fuel/air combustor with tangential admission |
US5572862A (en) | 1993-07-07 | 1996-11-12 | Mowill Rolf Jan | Convectively cooled, single stage, fully premixed fuel/air combustor for gas turbine engine modules |
US5628182A (en) | 1993-07-07 | 1997-05-13 | Mowill; R. Jan | Star combustor with dilution ports in can portions |
PL171012B1 (pl) | 1993-07-08 | 1997-02-28 | Waclaw Borszynski | Uklad do mokrego oczyszczania spalin z procesów spalania, korzystnie wegla, koksu,oleju opalowego PL |
US5794431A (en) | 1993-07-14 | 1998-08-18 | Hitachi, Ltd. | Exhaust recirculation type combined plant |
US5535584A (en) | 1993-10-19 | 1996-07-16 | California Energy Commission | Performance enhanced gas turbine powerplants |
US5345756A (en) | 1993-10-20 | 1994-09-13 | Texaco Inc. | Partial oxidation process with production of power |
US5394688A (en) | 1993-10-27 | 1995-03-07 | Westinghouse Electric Corporation | Gas turbine combustor swirl vane arrangement |
KR100370910B1 (ko) | 1993-12-10 | 2003-03-31 | 트랙테블 엘엔지 노쓰 아메리카 엘엘씨 | Lng조합싸이클플랜트시스템및조합싸이클플랜트의용량및효율을향상하기위한방법 |
US5542840A (en) | 1994-01-26 | 1996-08-06 | Zeeco Inc. | Burner for combusting gas and/or liquid fuel with low NOx production |
US5458481A (en) | 1994-01-26 | 1995-10-17 | Zeeco, Inc. | Burner for combusting gas with low NOx production |
NO180520C (no) | 1994-02-15 | 1997-05-07 | Kvaerner Asa | Fremgangsmåte til fjerning av karbondioksid fra forbrenningsgasser |
JP2950720B2 (ja) | 1994-02-24 | 1999-09-20 | 株式会社東芝 | ガスタービン燃焼装置およびその燃焼制御方法 |
US5439054A (en) | 1994-04-01 | 1995-08-08 | Amoco Corporation | Method for treating a mixture of gaseous fluids within a solid carbonaceous subterranean formation |
DE4411624A1 (de) | 1994-04-02 | 1995-10-05 | Abb Management Ag | Brennkammer mit Vormischbrennern |
US5581998A (en) | 1994-06-22 | 1996-12-10 | Craig; Joe D. | Biomass fuel turbine combuster |
US5402847A (en) | 1994-07-22 | 1995-04-04 | Conoco Inc. | Coal bed methane recovery |
US5599179A (en) * | 1994-08-01 | 1997-02-04 | Mississippi State University | Real-time combustion controller |
CA2198252C (en) | 1994-08-25 | 2005-05-10 | Rudi Beichel | Reduced pollution power generation system and gas generator therefore |
US5640840A (en) | 1994-12-12 | 1997-06-24 | Westinghouse Electric Corporation | Recuperative steam cooled gas turbine method and apparatus |
US5740667A (en) * | 1994-12-15 | 1998-04-21 | Amoco Corporation | Process for abatement of nitrogen oxides in exhaust from gas turbine power generation |
US5836164A (en) | 1995-01-30 | 1998-11-17 | Hitachi, Ltd. | Gas turbine combustor |
US5595059A (en) * | 1995-03-02 | 1997-01-21 | Westingthouse Electric Corporation | Combined cycle power plant with thermochemical recuperation and flue gas recirculation |
US5657631A (en) | 1995-03-13 | 1997-08-19 | B.B.A. Research & Development, Inc. | Injector for turbine engines |
WO1996030637A1 (en) | 1995-03-24 | 1996-10-03 | Ultimate Power Engineering Group, Inc. | High vanadium content fuel combustor and system |
US5685158A (en) | 1995-03-31 | 1997-11-11 | General Electric Company | Compressor rotor cooling system for a gas turbine |
CN1112505C (zh) | 1995-06-01 | 2003-06-25 | 特雷克特贝尔Lng北美公司 | 液化天然气作燃料的混合循环发电装置及液化天然气作燃料的燃气轮机 |
JPH09119641A (ja) | 1995-06-05 | 1997-05-06 | Allison Engine Co Inc | ガスタービンエンジン用低窒素酸化物希薄予混合モジュール |
US6170264B1 (en) | 1997-09-22 | 2001-01-09 | Clean Energy Systems, Inc. | Hydrocarbon combustion power generation system with CO2 sequestration |
WO1996041942A1 (de) | 1995-06-12 | 1996-12-27 | Gachnang, Hans, Rudolf | Verfahren zum zumischen von brenngas und vorrichtung zum zumischen von brenngas |
US5722230A (en) | 1995-08-08 | 1998-03-03 | General Electric Co. | Center burner in a multi-burner combustor |
US5644911A (en) * | 1995-08-10 | 1997-07-08 | Westinghouse Electric Corporation | Hydrogen-fueled semi-closed steam turbine power plant |
US5724805A (en) | 1995-08-21 | 1998-03-10 | University Of Massachusetts-Lowell | Power plant with carbon dioxide capture and zero pollutant emissions |
US5725054A (en) | 1995-08-22 | 1998-03-10 | Board Of Supervisors Of Louisiana State University And Agricultural & Mechanical College | Enhancement of residual oil recovery using a mixture of nitrogen or methane diluted with carbon dioxide in a single-well injection process |
US5638675A (en) | 1995-09-08 | 1997-06-17 | United Technologies Corporation | Double lobed mixer with major and minor lobes |
GB9520002D0 (en) | 1995-09-30 | 1995-12-06 | Rolls Royce Plc | Turbine engine control system |
DE19539774A1 (de) | 1995-10-26 | 1997-04-30 | Asea Brown Boveri | Zwischengekühlter Verdichter |
DK0870100T3 (da) | 1995-12-27 | 2000-07-17 | Shell Int Research | Flammeløs forbrændingsindretning |
DE19549143A1 (de) | 1995-12-29 | 1997-07-03 | Abb Research Ltd | Gasturbinenringbrennkammer |
US6201029B1 (en) | 1996-02-13 | 2001-03-13 | Marathon Oil Company | Staged combustion of a low heating value fuel gas for driving a gas turbine |
US5669958A (en) | 1996-02-29 | 1997-09-23 | Membrane Technology And Research, Inc. | Methane/nitrogen separation process |
GB2311596B (en) | 1996-03-29 | 2000-07-12 | Europ Gas Turbines Ltd | Combustor for gas - or liquid - fuelled turbine |
DE19618868C2 (de) | 1996-05-10 | 1998-07-02 | Daimler Benz Ag | Brennkraftmaschine mit einem Abgasrückführsystem |
US5930990A (en) | 1996-05-14 | 1999-08-03 | The Dow Chemical Company | Method and apparatus for achieving power augmentation in gas turbines via wet compression |
US5901547A (en) | 1996-06-03 | 1999-05-11 | Air Products And Chemicals, Inc. | Operation method for integrated gasification combined cycle power generation system |
US5950417A (en) | 1996-07-19 | 1999-09-14 | Foster Wheeler Energy International Inc. | Topping combustor for low oxygen vitiated air streams |
JPH10259736A (ja) | 1997-03-19 | 1998-09-29 | Mitsubishi Heavy Ind Ltd | 低NOx燃焼器 |
US5850732A (en) | 1997-05-13 | 1998-12-22 | Capstone Turbine Corporation | Low emissions combustion system for a gas turbine engine |
US5937634A (en) | 1997-05-30 | 1999-08-17 | Solar Turbines Inc | Emission control for a gas turbine engine |
US6062026A (en) | 1997-05-30 | 2000-05-16 | Turbodyne Systems, Inc. | Turbocharging systems for internal combustion engines |
NO308400B1 (no) | 1997-06-06 | 2000-09-11 | Norsk Hydro As | Kraftgenereringsprosess omfattende en forbrenningsprosess |
NO308399B1 (no) | 1997-06-06 | 2000-09-11 | Norsk Hydro As | Prosess for generering av kraft og/eller varme |
US6256976B1 (en) | 1997-06-27 | 2001-07-10 | Hitachi, Ltd. | Exhaust gas recirculation type combined plant |
US5771867A (en) | 1997-07-03 | 1998-06-30 | Caterpillar Inc. | Control system for exhaust gas recovery system in an internal combustion engine |
US5771868A (en) | 1997-07-03 | 1998-06-30 | Turbodyne Systems, Inc. | Turbocharging systems for internal combustion engines |
SE9702830D0 (sv) | 1997-07-31 | 1997-07-31 | Nonox Eng Ab | Environment friendly high efficiency power generation method based on gaseous fuels and a combined cycle with a nitrogen free gas turbine and a conventional steam turbine |
US6079974A (en) | 1997-10-14 | 2000-06-27 | Beloit Technologies, Inc. | Combustion chamber to accommodate a split-stream of recycled gases |
US6360528B1 (en) | 1997-10-31 | 2002-03-26 | General Electric Company | Chevron exhaust nozzle for a gas turbine engine |
US6000222A (en) | 1997-12-18 | 1999-12-14 | Allied Signal Inc. | Turbocharger with integral turbine exhaust gas recirculation control valve and exhaust gas bypass valve |
DE59811106D1 (de) | 1998-02-25 | 2004-05-06 | Alstom Technology Ltd Baden | Kraftwerksanlage und Verfahren zum Betrieb einer Kraftwerksanlage mit einem CO2-Prozess |
US6082113A (en) | 1998-05-22 | 2000-07-04 | Pratt & Whitney Canada Corp. | Gas turbine fuel injector |
US6082093A (en) | 1998-05-27 | 2000-07-04 | Solar Turbines Inc. | Combustion air control system for a gas turbine engine |
NO982504D0 (no) | 1998-06-02 | 1998-06-02 | Aker Eng As | Fjerning av CO2 i r°kgass |
US6244338B1 (en) | 1998-06-23 | 2001-06-12 | The University Of Wyoming Research Corp., | System for improving coalbed gas production |
US7717173B2 (en) | 1998-07-06 | 2010-05-18 | Ecycling, LLC | Methods of improving oil or gas production with recycled, increased sodium water |
US6089855A (en) | 1998-07-10 | 2000-07-18 | Thermo Power Corporation | Low NOx multistage combustor |
US6125627A (en) | 1998-08-11 | 2000-10-03 | Allison Advanced Development Company | Method and apparatus for spraying fuel within a gas turbine engine |
US6148602A (en) | 1998-08-12 | 2000-11-21 | Norther Research & Engineering Corporation | Solid-fueled power generation system with carbon dioxide sequestration and method therefor |
GB9818160D0 (en) | 1998-08-21 | 1998-10-14 | Rolls Royce Plc | A combustion chamber |
US6314721B1 (en) | 1998-09-04 | 2001-11-13 | United Technologies Corporation | Tabbed nozzle for jet noise suppression |
NO319681B1 (no) | 1998-09-16 | 2005-09-05 | Statoil Asa | Fremgangsmate for fremstilling av en H2-rik gass og en CO2-rik gass ved hoyt trykk |
NO317870B1 (no) | 1998-09-16 | 2004-12-27 | Statoil Asa | Fremgangsmate for a fremstille en H<N>2</N>-rik gass og en CO<N>2</N>-rik gass ved hoyt trykk |
US6370870B1 (en) | 1998-10-14 | 2002-04-16 | Nissan Motor Co., Ltd. | Exhaust gas purifying device |
NO984956D0 (no) | 1998-10-23 | 1998-10-23 | Nyfotek As | Brenner |
US5968349A (en) | 1998-11-16 | 1999-10-19 | Bhp Minerals International Inc. | Extraction of bitumen from bitumen froth and biotreatment of bitumen froth tailings generated from tar sands |
US6230103B1 (en) | 1998-11-18 | 2001-05-08 | Power Tech Associates, Inc. | Method of determining concentration of exhaust components in a gas turbine engine |
NO308401B1 (no) | 1998-12-04 | 2000-09-11 | Norsk Hydro As | FremgangsmÕte for gjenvinning av CO2 som genereres i en forbrenningsprosess samt anvendelse derav |
DE19857234C2 (de) | 1998-12-11 | 2000-09-28 | Daimler Chrysler Ag | Vorrichtung zur Abgasrückführung |
US6216549B1 (en) | 1998-12-11 | 2001-04-17 | The United States Of America As Represented By The Secretary Of The Interior | Collapsible bag sediment/water quality flow-weighted sampler |
EP1141534B1 (en) | 1999-01-04 | 2005-04-06 | Allison Advanced Development Company | Exhaust mixer and apparatus using same |
US6183241B1 (en) | 1999-02-10 | 2001-02-06 | Midwest Research Institute | Uniform-burning matrix burner |
NO990812L (no) | 1999-02-19 | 2000-08-21 | Norsk Hydro As | Metode for Õ fjerne og gjenvinne CO2 fra eksosgass |
US6276171B1 (en) | 1999-04-05 | 2001-08-21 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Integrated apparatus for generating power and/or oxygen enriched fluid, process for the operation thereof |
US6202442B1 (en) | 1999-04-05 | 2001-03-20 | L'air Liquide, Societe Anonyme Pour L'etude Et L'expoitation Des Procedes Georges Claude | Integrated apparatus for generating power and/or oxygen enriched fluid and process for the operation thereof |
FI105829B (fi) | 1999-05-14 | 2000-10-13 | Outokumpu Oy | Menetelmä kuparin uuttamiseksi vesiliuoksista |
GB9911867D0 (en) | 1999-05-22 | 1999-07-21 | Rolls Royce Plc | A combustion chamber assembly and a method of operating a combustion chamber assembly |
US6305929B1 (en) | 1999-05-24 | 2001-10-23 | Suk Ho Chung | Laser-induced ignition system using a cavity |
JP2000337107A (ja) | 1999-05-27 | 2000-12-05 | Mitsubishi Heavy Ind Ltd | クローズドガスタービンプラント |
US6283087B1 (en) | 1999-06-01 | 2001-09-04 | Kjell Isaksen | Enhanced method of closed vessel combustion |
US6256994B1 (en) | 1999-06-04 | 2001-07-10 | Air Products And Chemicals, Inc. | Operation of an air separation process with a combustion engine for the production of atmospheric gas products and electric power |
US6345493B1 (en) | 1999-06-04 | 2002-02-12 | Air Products And Chemicals, Inc. | Air separation process and system with gas turbine drivers |
US6263659B1 (en) | 1999-06-04 | 2001-07-24 | Air Products And Chemicals, Inc. | Air separation process integrated with gas turbine combustion engine driver |
US7065953B1 (en) | 1999-06-10 | 2006-06-27 | Enhanced Turbine Output Holding | Supercharging system for gas turbines |
US6324867B1 (en) | 1999-06-15 | 2001-12-04 | Exxonmobil Oil Corporation | Process and system for liquefying natural gas |
SE9902491L (sv) | 1999-06-30 | 2000-12-31 | Saab Automobile | Förbränningsmotor med avgasåtermatning |
US6202574B1 (en) | 1999-07-09 | 2001-03-20 | Abb Alstom Power Inc. | Combustion method and apparatus for producing a carbon dioxide end product |
US6301888B1 (en) | 1999-07-22 | 2001-10-16 | The United States Of America As Represented By The Administrator Of The Environmental Protection Agency | Low emission, diesel-cycle engine |
US6367258B1 (en) | 1999-07-22 | 2002-04-09 | Bechtel Corporation | Method and apparatus for vaporizing liquid natural gas in a combined cycle power plant |
US6248794B1 (en) | 1999-08-05 | 2001-06-19 | Atlantic Richfield Company | Integrated process for converting hydrocarbon gas to liquids |
WO2001011215A1 (en) | 1999-08-09 | 2001-02-15 | Technion Research And Development Foundation Ltd. | Novel design of adiabatic combustors |
US6101983A (en) | 1999-08-11 | 2000-08-15 | General Electric Co. | Modified gas turbine system with advanced pressurized fluidized bed combustor cycle |
EP1217299B1 (en) | 1999-08-16 | 2011-11-16 | Nippon Furnace Co., Ltd. | Device and method for feeding fuel |
US7015271B2 (en) | 1999-08-19 | 2006-03-21 | Ppg Industries Ohio, Inc. | Hydrophobic particulate inorganic oxides and polymeric compositions containing same |
WO2001018371A1 (en) | 1999-09-07 | 2001-03-15 | Geza Vermes | Ambient pressure gas turbine system |
DE19944922A1 (de) | 1999-09-20 | 2001-03-22 | Asea Brown Boveri | Steuerung von Primärmassnahmen zur Reduktion der thermischen Stickoxidbildung in Gasturbinen |
DE19949739C1 (de) | 1999-10-15 | 2001-08-23 | Karlsruhe Forschzent | Massesensitiver Sensor |
US6383461B1 (en) | 1999-10-26 | 2002-05-07 | John Zink Company, Llc | Fuel dilution methods and apparatus for NOx reduction |
US20010004838A1 (en) | 1999-10-29 | 2001-06-28 | Wong Kenneth Kai | Integrated heat exchanger system for producing carbon dioxide |
US6299433B1 (en) * | 1999-11-05 | 2001-10-09 | Gas Research Institute | Burner control |
US6298652B1 (en) | 1999-12-13 | 2001-10-09 | Exxon Mobil Chemical Patents Inc. | Method for utilizing gas reserves with low methane concentrations and high inert gas concentrations for fueling gas turbines |
US6266954B1 (en) | 1999-12-15 | 2001-07-31 | General Electric Co. | Double wall bearing cone |
US6484503B1 (en) | 2000-01-12 | 2002-11-26 | Arie Raz | Compression and condensation of turbine exhaust steam |
DE10001110A1 (de) | 2000-01-13 | 2001-08-16 | Alstom Power Schweiz Ag Baden | Verfahren zur Rückgewinnung von Wasser aus dem Rauchgas eines Kombikraftwerkes sowie Kombikraftwerk zur Durchführung des Verfahrens |
DE10001997A1 (de) | 2000-01-19 | 2001-07-26 | Alstom Power Schweiz Ag Baden | Verbund-Kraftwerk sowie Verfahren zum Betrieb eines solchen Verbund-Kraftwerkes |
US6247315B1 (en) | 2000-03-08 | 2001-06-19 | American Air Liquids, Inc. | Oxidant control in co-generation installations |
US6247316B1 (en) | 2000-03-22 | 2001-06-19 | Clean Energy Systems, Inc. | Clean air engines for transportation and other power applications |
US6405536B1 (en) | 2000-03-27 | 2002-06-18 | Wu-Chi Ho | Gas turbine combustor burning LBTU fuel gas |
US6508209B1 (en) | 2000-04-03 | 2003-01-21 | R. Kirk Collier, Jr. | Reformed natural gas for powering an internal combustion engine |
US7011154B2 (en) | 2000-04-24 | 2006-03-14 | Shell Oil Company | In situ recovery from a kerogen and liquid hydrocarbon containing formation |
FR2808223B1 (fr) | 2000-04-27 | 2002-11-22 | Inst Francais Du Petrole | Procede de purification d'un effluent contenant du gaz carbonique et des hydrocarbures par combustion |
SE523342C2 (sv) | 2000-05-02 | 2004-04-13 | Volvo Teknisk Utveckling Ab | Anordning och förfarande för reduktion av en gaskomponent i en avgasström från en förbränningsmotor |
CA2409700C (en) | 2000-05-12 | 2010-02-09 | Clean Energy Systems, Inc. | Semi-closed brayton cycle gas turbine power systems |
US6429020B1 (en) | 2000-06-02 | 2002-08-06 | The United States Of America As Represented By The United States Department Of Energy | Flashback detection sensor for lean premix fuel nozzles |
JP3864671B2 (ja) | 2000-06-12 | 2007-01-10 | 日産自動車株式会社 | ディーゼルエンジンの燃料噴射制御装置 |
US6374594B1 (en) | 2000-07-12 | 2002-04-23 | Power Systems Mfg., Llc | Silo/can-annular low emissions combustor |
US6282901B1 (en) | 2000-07-19 | 2001-09-04 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Integrated air separation process |
US6502383B1 (en) | 2000-08-31 | 2003-01-07 | General Electric Company | Stub airfoil exhaust nozzle |
US6301889B1 (en) | 2000-09-21 | 2001-10-16 | Caterpillar Inc. | Turbocharger with exhaust gas recirculation |
DE10049040A1 (de) | 2000-10-04 | 2002-06-13 | Alstom Switzerland Ltd | Verfahren zur Regeneration einer Katalysatoranlage und Vorrichtung zur Durchführung des Verfahrens |
DE10049912A1 (de) | 2000-10-10 | 2002-04-11 | Daimler Chrysler Ag | Brennkraftmaschine mit Abgasturbolader und Compound-Nutzturbine |
DE10050248A1 (de) | 2000-10-11 | 2002-04-18 | Alstom Switzerland Ltd | Brenner |
GB0025552D0 (en) | 2000-10-18 | 2000-11-29 | Air Prod & Chem | Process and apparatus for the generation of power |
US7097925B2 (en) | 2000-10-30 | 2006-08-29 | Questair Technologies Inc. | High temperature fuel cell power plant |
US6412278B1 (en) | 2000-11-10 | 2002-07-02 | Borgwarner, Inc. | Hydraulically powered exhaust gas recirculation system |
US6412559B1 (en) | 2000-11-24 | 2002-07-02 | Alberta Research Council Inc. | Process for recovering methane and/or sequestering fluids |
DE10064270A1 (de) | 2000-12-22 | 2002-07-11 | Alstom Switzerland Ltd | Verfahren zum Betrieb einer Gasturbinenanlage sowie eine diesbezügliche Gasturbinenanlage |
WO2002055851A1 (en) | 2001-01-08 | 2002-07-18 | Catalytica Energy Systems, Inc. | CATALYST PLACEMENT IN COMBUSTION CYLINDER FOR REDUCTION OF NOx AND PARTICULATE SOOT |
US6467270B2 (en) | 2001-01-31 | 2002-10-22 | Cummins Inc. | Exhaust gas recirculation air handling system for an internal combustion engine |
US6715916B2 (en) | 2001-02-08 | 2004-04-06 | General Electric Company | System and method for determining gas turbine firing and combustion reference temperatures having correction for water content in fuel |
US6490858B2 (en) | 2001-02-16 | 2002-12-10 | Ashley J. Barrett | Catalytic converter thermal aging method and apparatus |
US6606861B2 (en) | 2001-02-26 | 2003-08-19 | United Technologies Corporation | Low emissions combustor for a gas turbine engine |
US7578132B2 (en) | 2001-03-03 | 2009-08-25 | Rolls-Royce Plc | Gas turbine engine exhaust nozzle |
US6821501B2 (en) | 2001-03-05 | 2004-11-23 | Shell Oil Company | Integrated flameless distributed combustion/steam reforming membrane reactor for hydrogen production and use thereof in zero emissions hybrid power system |
US6412302B1 (en) | 2001-03-06 | 2002-07-02 | Abb Lummus Global, Inc. - Randall Division | LNG production using dual independent expander refrigeration cycles |
US6499990B1 (en) | 2001-03-07 | 2002-12-31 | Zeeco, Inc. | Low NOx burner apparatus and method |
GB2373299B (en) | 2001-03-12 | 2004-10-27 | Alstom Power Nv | Re-fired gas turbine engine |
EP1378627B1 (en) | 2001-03-15 | 2008-07-02 | Alexei Leonidovich Zapadinski | Method for developing a hydrocarbon reservoir (variants) and complex for carrying out said method (variants) |
US6732531B2 (en) | 2001-03-16 | 2004-05-11 | Capstone Turbine Corporation | Combustion system for a gas turbine engine with variable airflow pressure actuated premix injector |
US6615576B2 (en) | 2001-03-29 | 2003-09-09 | Honeywell International Inc. | Tortuous path quiet exhaust eductor system |
US6487863B1 (en) | 2001-03-30 | 2002-12-03 | Siemens Westinghouse Power Corporation | Method and apparatus for cooling high temperature components in a gas turbine |
US6782947B2 (en) | 2001-04-24 | 2004-08-31 | Shell Oil Company | In situ thermal processing of a relatively impermeable formation to increase permeability of the formation |
US6991036B2 (en) | 2001-04-24 | 2006-01-31 | Shell Oil Company | Thermal processing of a relatively permeable formation |
JP3972599B2 (ja) | 2001-04-27 | 2007-09-05 | 日産自動車株式会社 | ディーゼルエンジンの制御装置 |
US6868677B2 (en) | 2001-05-24 | 2005-03-22 | Clean Energy Systems, Inc. | Combined fuel cell and fuel combustion power generation systems |
WO2002097252A1 (en) | 2001-05-30 | 2002-12-05 | Conoco Inc. | Lng regasification process and system |
EP1262714A1 (de) | 2001-06-01 | 2002-12-04 | ALSTOM (Switzerland) Ltd | Brenner mit Abgasrückführung |
US6484507B1 (en) | 2001-06-05 | 2002-11-26 | Louis A. Pradt | Method and apparatus for controlling liquid droplet size and quantity in a stream of gas |
US6622645B2 (en) | 2001-06-15 | 2003-09-23 | Honeywell International Inc. | Combustion optimization with inferential sensor |
DE10131798A1 (de) | 2001-06-30 | 2003-01-16 | Daimler Chrysler Ag | Kraftfahrzeug mit Aktivkohlefilter und Verfahren zur Regeneration eines Aktivkohlefilters |
US6813889B2 (en) | 2001-08-29 | 2004-11-09 | Hitachi, Ltd. | Gas turbine combustor and operating method thereof |
WO2003021017A1 (en) | 2001-08-30 | 2003-03-13 | Tda Research, Inc. | Process for the removal of impurities from combustion fullerenes |
WO2003018958A1 (en) | 2001-08-31 | 2003-03-06 | Statoil Asa | Method and plant for enhanced oil recovery and simultaneous synthesis of hydrocarbons from natural gas |
JP2003090250A (ja) | 2001-09-18 | 2003-03-28 | Nissan Motor Co Ltd | ディーゼルエンジンの制御装置 |
WO2003027461A1 (de) | 2001-09-24 | 2003-04-03 | Alstom Technology Ltd | Gasturbinenanlage für ein arbeitsmedium in form eines kohlendioxid/wasser-gemisches |
US6640548B2 (en) | 2001-09-26 | 2003-11-04 | Siemens Westinghouse Power Corporation | Apparatus and method for combusting low quality fuel |
WO2003029618A1 (de) | 2001-10-01 | 2003-04-10 | Alstom Technology Ltd. | Verfahren und vorrichtung zum anfahren von emissionsfreien gasturbinenkraftwerken |
US6969123B2 (en) | 2001-10-24 | 2005-11-29 | Shell Oil Company | Upgrading and mining of coal |
US7077199B2 (en) | 2001-10-24 | 2006-07-18 | Shell Oil Company | In situ thermal processing of an oil reservoir formation |
US7104319B2 (en) | 2001-10-24 | 2006-09-12 | Shell Oil Company | In situ thermal processing of a heavy oil diatomite formation |
DE10152803A1 (de) | 2001-10-25 | 2003-05-15 | Daimler Chrysler Ag | Brennkraftmaschine mit einem Abgasturbolader und einer Abgasrückführungsvorrichtung |
JP2005516141A (ja) | 2001-10-26 | 2005-06-02 | アルストム テクノロジー リミテッド | 高排気ガス再循環率で動作するように構成したガスタービンとその動作方法 |
US7143572B2 (en) | 2001-11-09 | 2006-12-05 | Kawasaki Jukogyo Kabushiki Kaisha | Gas turbine system comprising closed system of fuel and combustion gas using underground coal layer |
US6790030B2 (en) * | 2001-11-20 | 2004-09-14 | The Regents Of The University Of California | Multi-stage combustion using nitrogen-enriched air |
US6505567B1 (en) | 2001-11-26 | 2003-01-14 | Alstom (Switzerland) Ltd | Oxygen fired circulating fluidized bed steam generator |
CA2468769A1 (en) | 2001-12-03 | 2003-06-12 | Clean Energy Systems, Inc. | Coal and syngas fueled power generation systems featuring zero atmospheric emissions |
GB2382847A (en) | 2001-12-06 | 2003-06-11 | Alstom | Gas turbine wet compression |
US20030134241A1 (en) | 2002-01-14 | 2003-07-17 | Ovidiu Marin | Process and apparatus of combustion for reduction of nitrogen oxide emissions |
US6743829B2 (en) | 2002-01-18 | 2004-06-01 | Bp Corporation North America Inc. | Integrated processing of natural gas into liquid products |
US6722436B2 (en) | 2002-01-25 | 2004-04-20 | Precision Drilling Technology Services Group Inc. | Apparatus and method for operating an internal combustion engine to reduce free oxygen contained within engine exhaust gas |
US6752620B2 (en) | 2002-01-31 | 2004-06-22 | Air Products And Chemicals, Inc. | Large scale vortex devices for improved burner operation |
US6725665B2 (en) | 2002-02-04 | 2004-04-27 | Alstom Technology Ltd | Method of operation of gas turbine having multiple burners |
US6745624B2 (en) | 2002-02-05 | 2004-06-08 | Ford Global Technologies, Llc | Method and system for calibrating a tire pressure sensing system for an automotive vehicle |
US7284362B2 (en) | 2002-02-11 | 2007-10-23 | L'Air Liquide, Société Anonyme à Directoire et Conseil de Surveillance pour l'Étude et l'Exploitation des Procedes Georges Claude | Integrated air separation and oxygen fired power generation system |
US6823852B2 (en) | 2002-02-19 | 2004-11-30 | Collier Technologies, Llc | Low-emission internal combustion engine |
US7313916B2 (en) | 2002-03-22 | 2008-01-01 | Philip Morris Usa Inc. | Method and apparatus for generating power by combustion of vaporized fuel |
US6532745B1 (en) | 2002-04-10 | 2003-03-18 | David L. Neary | Partially-open gas turbine cycle providing high thermal efficiencies and ultra-low emissions |
DE60313392T2 (de) | 2002-05-16 | 2007-08-09 | Rolls-Royce Plc | Gasturbine |
US6644041B1 (en) | 2002-06-03 | 2003-11-11 | Volker Eyermann | System in process for the vaporization of liquefied natural gas |
US7491250B2 (en) | 2002-06-25 | 2009-02-17 | Exxonmobil Research And Engineering Company | Pressure swing reforming |
GB2390150A (en) | 2002-06-26 | 2003-12-31 | Alstom | Reheat combustion system for a gas turbine including an accoustic screen |
US6702570B2 (en) | 2002-06-28 | 2004-03-09 | Praxair Technology Inc. | Firing method for a heat consuming device utilizing oxy-fuel combustion |
US6748004B2 (en) | 2002-07-25 | 2004-06-08 | Air Liquide America, L.P. | Methods and apparatus for improved energy efficient control of an electric arc furnace fume extraction system |
US6772583B2 (en) | 2002-09-11 | 2004-08-10 | Siemens Westinghouse Power Corporation | Can combustor for a gas turbine engine |
US6826913B2 (en) | 2002-10-31 | 2004-12-07 | Honeywell International Inc. | Airflow modulation technique for low emissions combustors |
US7143606B2 (en) | 2002-11-01 | 2006-12-05 | L'air Liquide-Societe Anonyme A'directoire Et Conseil De Surveillance Pour L'etide Et L'exploitation Des Procedes Georges Claude | Combined air separation natural gas liquefaction plant |
EP1561010B1 (en) | 2002-11-08 | 2012-09-05 | Alstom Technology Ltd | Gas turbine power plant and method of operating the same |
US6945029B2 (en) | 2002-11-15 | 2005-09-20 | Clean Energy Systems, Inc. | Low pollution power generation system with ion transfer membrane air separation |
GB0226983D0 (en) | 2002-11-19 | 2002-12-24 | Boc Group Plc | Nitrogen rejection method and apparatus |
DE10257704A1 (de) | 2002-12-11 | 2004-07-15 | Alstom Technology Ltd | Verfahren zur Verbrennung eines Brennstoffs |
WO2004055322A1 (en) | 2002-12-13 | 2004-07-01 | Statoil Asa | A method for oil recovery from an oil field |
NO20026021D0 (no) | 2002-12-13 | 2002-12-13 | Statoil Asa I & K Ir Pat | Fremgangsmåte for ökt oljeutvinning |
US6731501B1 (en) | 2003-01-03 | 2004-05-04 | Jian-Roung Cheng | Heat dissipating device for dissipating heat generated by a disk drive module inside a computer housing |
US6851413B1 (en) | 2003-01-10 | 2005-02-08 | Ronnell Company, Inc. | Method and apparatus to increase combustion efficiency and to reduce exhaust gas pollutants from combustion of a fuel |
US6929423B2 (en) | 2003-01-16 | 2005-08-16 | Paul A. Kittle | Gas recovery from landfills using aqueous foam |
BRPI0406806A (pt) | 2003-01-17 | 2005-12-27 | Catalytica Energy Sys Inc | Sistema e método de controle dinâmico para multicombustor catalìtico para motor de turbina a gás |
CN1761588A (zh) | 2003-01-22 | 2006-04-19 | 瓦斯特能量系统有限公司 | 使用热稀释剂的热力学循环 |
US8631657B2 (en) | 2003-01-22 | 2014-01-21 | Vast Power Portfolio, Llc | Thermodynamic cycles with thermal diluent |
US9254729B2 (en) | 2003-01-22 | 2016-02-09 | Vast Power Portfolio, Llc | Partial load combustion cycles |
US6820428B2 (en) | 2003-01-30 | 2004-11-23 | Wylie Inventions Company, Inc. | Supercritical combined cycle for generating electric power |
GB2398863B (en) | 2003-01-31 | 2007-10-17 | Alstom | Combustion Chamber |
US6675579B1 (en) | 2003-02-06 | 2004-01-13 | Ford Global Technologies, Llc | HCCI engine intake/exhaust systems for fast inlet temperature and pressure control with intake pressure boosting |
US7618606B2 (en) | 2003-02-06 | 2009-11-17 | The Ohio State University | Separation of carbon dioxide (CO2) from gas mixtures |
WO2004072443A1 (en) * | 2003-02-11 | 2004-08-26 | Statoil Asa | Efficient combined cycle power plant with co2 capture and a combustor arrangement with separate flows |
US7914764B2 (en) | 2003-02-28 | 2011-03-29 | Exxonmobil Research And Engineering Company | Hydrogen manufacture using pressure swing reforming |
US7053128B2 (en) | 2003-02-28 | 2006-05-30 | Exxonmobil Research And Engineering Company | Hydrocarbon synthesis process using pressure swing reforming |
US7217303B2 (en) | 2003-02-28 | 2007-05-15 | Exxonmobil Research And Engineering Company | Pressure swing reforming for fuel cell systems |
US7045553B2 (en) | 2003-02-28 | 2006-05-16 | Exxonmobil Research And Engineering Company | Hydrocarbon synthesis process using pressure swing reforming |
US20040170559A1 (en) | 2003-02-28 | 2004-09-02 | Frank Hershkowitz | Hydrogen manufacture using pressure swing reforming |
US7637093B2 (en) | 2003-03-18 | 2009-12-29 | Fluor Technologies Corporation | Humid air turbine cycle with carbon dioxide recovery |
US7401577B2 (en) | 2003-03-19 | 2008-07-22 | American Air Liquide, Inc. | Real time optimization and control of oxygen enhanced boilers |
US7074033B2 (en) | 2003-03-22 | 2006-07-11 | David Lloyd Neary | Partially-open fired heater cycle providing high thermal efficiencies and ultra-low emissions |
US7168265B2 (en) | 2003-03-27 | 2007-01-30 | Bp Corporation North America Inc. | Integrated processing of natural gas into liquid products |
WO2004085816A1 (de) | 2003-03-28 | 2004-10-07 | Siemens Aktiengesellschaft | TEMPERATURMESSEINRICHTUNG UND REGELUNG FÜR DIE HEIßGASTEMPERATUR EINER GASTURBINE |
JP2004324618A (ja) * | 2003-04-28 | 2004-11-18 | Kawasaki Heavy Ind Ltd | 吸気流量制御機構付きガスタービンエンジン |
WO2004097297A1 (en) | 2003-04-29 | 2004-11-11 | Her Majesty The Queen In Right Of Canada As Represented By The Minister Of Natural Resources | In-situ capture of carbon dioxide and sulphur dioxide in a fluidized bed combustor |
CA2460292C (en) | 2003-05-08 | 2011-08-23 | Sulzer Chemtech Ag | A static mixer |
US7503948B2 (en) | 2003-05-23 | 2009-03-17 | Exxonmobil Research And Engineering Company | Solid oxide fuel cell systems having temperature swing reforming |
DE10325111A1 (de) | 2003-06-02 | 2005-01-05 | Alstom Technology Ltd | Verfahren zur Erzeugung von Energie in einer eine Gasturbine umfassende Energieerzeugungsanlage sowie Energieerzeugungsanlage zur Durchführung des Verfahrens |
US7056482B2 (en) | 2003-06-12 | 2006-06-06 | Cansolv Technologies Inc. | Method for recovery of CO2 from gas streams |
US7043898B2 (en) | 2003-06-23 | 2006-05-16 | Pratt & Whitney Canada Corp. | Combined exhaust duct and mixer for a gas turbine engine |
DE10334590B4 (de) | 2003-07-28 | 2006-10-26 | Uhde Gmbh | Verfahren zur Gewinnung von Wasserstoff aus einem methanhaltigen Gas, insbesondere Erdgas und Anlage zur Durchführung des Verfahrens |
US7007487B2 (en) * | 2003-07-31 | 2006-03-07 | Mes International, Inc. | Recuperated gas turbine engine system and method employing catalytic combustion |
GB0323255D0 (en) | 2003-10-04 | 2003-11-05 | Rolls Royce Plc | Method and system for controlling fuel supply in a combustion turbine engine |
DE10350044A1 (de) | 2003-10-27 | 2005-05-25 | Basf Ag | Verfahren zur Herstellung von 1-Buten |
US6904815B2 (en) | 2003-10-28 | 2005-06-14 | General Electric Company | Configurable multi-point sampling method and system for representative gas composition measurements in a stratified gas flow stream |
NO321817B1 (no) | 2003-11-06 | 2006-07-10 | Sargas As | Renseanlegg for varmekraftverk |
US6988549B1 (en) | 2003-11-14 | 2006-01-24 | John A Babcock | SAGD-plus |
US7032388B2 (en) | 2003-11-17 | 2006-04-25 | General Electric Company | Method and system for incorporating an emission sensor into a gas turbine controller |
US6939130B2 (en) | 2003-12-05 | 2005-09-06 | Gas Technology Institute | High-heat transfer low-NOx combustion system |
US7299619B2 (en) | 2003-12-13 | 2007-11-27 | Siemens Power Generation, Inc. | Vaporization of liquefied natural gas for increased efficiency in power cycles |
US7183328B2 (en) | 2003-12-17 | 2007-02-27 | Exxonmobil Chemical Patents Inc. | Methanol manufacture using pressure swing reforming |
US7124589B2 (en) | 2003-12-22 | 2006-10-24 | David Neary | Power cogeneration system and apparatus means for improved high thermal efficiencies and ultra-low emissions |
DE10360951A1 (de) | 2003-12-23 | 2005-07-28 | Alstom Technology Ltd | Wärmekraftanlage mit sequentieller Verbrennung und reduziertem CO2-Ausstoß sowie Verfahren zum Betreiben einer derartigen Anlage |
US20050144961A1 (en) | 2003-12-24 | 2005-07-07 | General Electric Company | System and method for cogeneration of hydrogen and electricity |
DE10361823A1 (de) | 2003-12-30 | 2005-08-11 | Basf Ag | Verfahren zur Herstellung von Butadien und 1-Buten |
DE10361824A1 (de) | 2003-12-30 | 2005-07-28 | Basf Ag | Verfahren zur Herstellung von Butadien |
US7096669B2 (en) | 2004-01-13 | 2006-08-29 | Compressor Controls Corp. | Method and apparatus for the prevention of critical process variable excursions in one or more turbomachines |
EP2402068B2 (en) | 2004-01-20 | 2016-11-16 | Fluor Technologies Corporation | Methods and configurations for acid gas enrichment |
US7305817B2 (en) | 2004-02-09 | 2007-12-11 | General Electric Company | Sinuous chevron exhaust nozzle |
JP2005226847A (ja) | 2004-02-10 | 2005-08-25 | Ebara Corp | 燃焼装置及び燃焼方法 |
US7468173B2 (en) | 2004-02-25 | 2008-12-23 | Sunstone Corporation | Method for producing nitrogen to use in under balanced drilling, secondary recovery production operations and pipeline maintenance |
DE102004009794A1 (de) | 2004-02-28 | 2005-09-22 | Daimlerchrysler Ag | Brennkraftmaschine mit zwei Abgasturboladern |
US8951951B2 (en) | 2004-03-02 | 2015-02-10 | Troxler Electronic Laboratories, Inc. | Solvent compositions for removing petroleum residue from a substrate and methods of use thereof |
US6971242B2 (en) | 2004-03-02 | 2005-12-06 | Caterpillar Inc. | Burner for a gas turbine engine |
US7752848B2 (en) | 2004-03-29 | 2010-07-13 | General Electric Company | System and method for co-production of hydrogen and electrical energy |
ATE389852T1 (de) | 2004-03-30 | 2008-04-15 | Alstom Technology Ltd | Vorrichtung und verfahren zur flammenstabilisierung in einem brenner |
EP1730447A1 (de) | 2004-03-31 | 2006-12-13 | Alstom Technology Ltd | Brenner |
WO2005100754A2 (en) | 2004-04-16 | 2005-10-27 | Clean Energy Systems, Inc. | Zero emissions closed rankine cycle power system |
US7302801B2 (en) | 2004-04-19 | 2007-12-04 | Hamilton Sundstrand Corporation | Lean-staged pyrospin combustor |
US7185497B2 (en) | 2004-05-04 | 2007-03-06 | Honeywell International, Inc. | Rich quick mix combustion system |
WO2005108865A1 (en) | 2004-05-06 | 2005-11-17 | New Power Concepts Llc | Gaseous fuel burner |
ITBO20040296A1 (it) | 2004-05-11 | 2004-08-11 | Itea Spa | Combustori ad alta efficienza e impatto ambientale ridotto, e procedimenti per la produzione di energia elettrica da esso derivabili |
US7438744B2 (en) | 2004-05-14 | 2008-10-21 | Eco/Technologies, Llc | Method and system for sequestering carbon emissions from a combustor/boiler |
US20080034727A1 (en) | 2004-05-19 | 2008-02-14 | Fluor Technologies Corporation | Triple Cycle Power Plant |
US7065972B2 (en) | 2004-05-21 | 2006-06-27 | Honeywell International, Inc. | Fuel-air mixing apparatus for reducing gas turbine combustor exhaust emissions |
US7010921B2 (en) | 2004-06-01 | 2006-03-14 | General Electric Company | Method and apparatus for cooling combustor liner and transition piece of a gas turbine |
US6993916B2 (en) | 2004-06-08 | 2006-02-07 | General Electric Company | Burner tube and method for mixing air and gas in a gas turbine engine |
US7197880B2 (en) | 2004-06-10 | 2007-04-03 | United States Department Of Energy | Lean blowoff detection sensor |
US7788897B2 (en) | 2004-06-11 | 2010-09-07 | Vast Power Portfolio, Llc | Low emissions combustion apparatus and method |
US7472550B2 (en) | 2004-06-14 | 2009-01-06 | University Of Florida Research Foundation, Inc. | Combined cooling and power plant with water extraction |
EP1781902A4 (en) | 2004-07-14 | 2009-08-12 | Fluor Tech Corp | CONFIGURATIONS AND METHOD FOR ENERGY EFFICIENCY WITH INTEGRATED LNG RE-GASIFICATION |
US7498009B2 (en) | 2004-08-16 | 2009-03-03 | Dana Uv, Inc. | Controlled spectrum ultraviolet radiation pollution control process |
DE102004039927A1 (de) | 2004-08-18 | 2006-02-23 | Daimlerchrysler Ag | Brennkraftmaschine mit einem Abgasturbolader und einer Abgasrückführeinrichtung |
DE102004040893A1 (de) | 2004-08-24 | 2006-03-02 | Bayerische Motoren Werke Ag | Abgasturbolader |
US7137623B2 (en) | 2004-09-17 | 2006-11-21 | Spx Cooling Technologies, Inc. | Heating tower apparatus and method with isolation of outlet and inlet air |
JP4905958B2 (ja) | 2004-09-29 | 2012-03-28 | 太平洋セメント株式会社 | セメントキルン燃焼ガス抽気ダストの処理システム及び処理方法 |
KR101178429B1 (ko) | 2004-09-29 | 2012-08-31 | 다이헤이요 세멘토 가부시키가이샤 | 시멘트 킬른 연소가스 추기 더스트의 처리 시스템 및 처리방법 |
JP4626251B2 (ja) | 2004-10-06 | 2011-02-02 | 株式会社日立製作所 | 燃焼器及び燃焼器の燃焼方法 |
US7381393B2 (en) | 2004-10-07 | 2008-06-03 | The Regents Of The University Of California | Process for sulfur removal suitable for treating high-pressure gas streams |
US7434384B2 (en) | 2004-10-25 | 2008-10-14 | United Technologies Corporation | Fluid mixer with an integral fluid capture ducts forming auxiliary secondary chutes at the discharge end of said ducts |
US7762084B2 (en) | 2004-11-12 | 2010-07-27 | Rolls-Royce Canada, Ltd. | System and method for controlling the working line position in a gas turbine engine compressor |
US7357857B2 (en) | 2004-11-29 | 2008-04-15 | Baker Hughes Incorporated | Process for extracting bitumen |
US7389635B2 (en) | 2004-12-01 | 2008-06-24 | Honeywell International Inc. | Twisted mixer with open center body |
US7506501B2 (en) | 2004-12-01 | 2009-03-24 | Honeywell International Inc. | Compact mixer with trimmable open centerbody |
EP1666822A1 (de) | 2004-12-03 | 2006-06-07 | Linde Aktiengesellschaft | Vorrichtung zur Tieftemperaturzerlegung eines Gasgemisches, insbesondere von Luft |
JP2006183599A (ja) | 2004-12-28 | 2006-07-13 | Nissan Motor Co Ltd | 内燃機関の排気浄化装置 |
ES2285577T3 (es) | 2005-01-17 | 2007-11-16 | Balcke-Durr Gmbh | Dispositivo y procedimiento para el mezclado de un fluido que circula en una direccion de circulacion. |
CN1847766A (zh) | 2005-02-11 | 2006-10-18 | 林德股份公司 | 通过与冷却液体直接热交换而冷却气体的方法和装置 |
US20060183009A1 (en) | 2005-02-11 | 2006-08-17 | Berlowitz Paul J | Fuel cell fuel processor with hydrogen buffering |
US7875402B2 (en) | 2005-02-23 | 2011-01-25 | Exxonmobil Research And Engineering Company | Proton conducting solid oxide fuel cell systems having temperature swing reforming |
US7137256B1 (en) | 2005-02-28 | 2006-11-21 | Peter Stuttaford | Method of operating a combustion system for increased turndown capability |
US20060196812A1 (en) | 2005-03-02 | 2006-09-07 | Beetge Jan H | Zone settling aid and method for producing dry diluted bitumen with reduced losses of asphaltenes |
US7194869B2 (en) | 2005-03-08 | 2007-03-27 | Siemens Power Generation, Inc. | Turbine exhaust water recovery system |
US20090117024A1 (en) | 2005-03-14 | 2009-05-07 | Geoffrey Gerald Weedon | Process for the Production of Hydrogen with Co-Production and Capture of Carbon Dioxide |
US7681394B2 (en) | 2005-03-25 | 2010-03-23 | The United States Of America, As Represented By The Administrator Of The U.S. Environmental Protection Agency | Control methods for low emission internal combustion system |
AU2006229877B2 (en) | 2005-03-30 | 2009-04-23 | Fluor Technologies Corporation | Integrated of LNG regasification with refinery and power generation |
JP4516620B2 (ja) | 2005-03-30 | 2010-08-04 | フルオー・テクノロジーズ・コーポレイシヨン | Lng再ガス化と発電プラントとの熱的統合のための構成および方法 |
DE102005015151A1 (de) * | 2005-03-31 | 2006-10-26 | Alstom Technology Ltd. | Gasturbinenanlage |
US7906304B2 (en) | 2005-04-05 | 2011-03-15 | Geosynfuels, Llc | Method and bioreactor for producing synfuel from carbonaceous material |
CA2603529A1 (en) | 2005-04-05 | 2006-10-12 | Sargas As | Low co2 thermal powerplant |
DE102005017905A1 (de) | 2005-04-18 | 2006-10-19 | Behr Gmbh & Co. Kg | Vorrichtung zur gekühlten Rückführung von Abgas einer Brennkraftmaschine eines Kraftfahrzeuges |
US7402038B2 (en) * | 2005-04-22 | 2008-07-22 | The North American Manufacturing Company, Ltd. | Combustion method and apparatus |
CA2823766C (en) | 2005-05-02 | 2015-06-23 | Vast Power Portfolio, Llc | Wet compression apparatus and method |
US7827782B2 (en) | 2005-05-19 | 2010-11-09 | Ford Global Technologies, Llc | Method for remediating emissions |
US7874350B2 (en) | 2005-05-23 | 2011-01-25 | Precision Combustion, Inc. | Reducing the energy requirements for the production of heavy oil |
US7789159B1 (en) | 2005-05-27 | 2010-09-07 | Bader Mansour S | Methods to de-sulfate saline streams |
US7980312B1 (en) | 2005-06-20 | 2011-07-19 | Hill Gilman A | Integrated in situ retorting and refining of oil shale |
US7914749B2 (en) | 2005-06-27 | 2011-03-29 | Solid Gas Technologies | Clathrate hydrate modular storage, applications and utilization processes |
US7966822B2 (en) | 2005-06-30 | 2011-06-28 | General Electric Company | Reverse-flow gas turbine combustion system |
US7481048B2 (en) | 2005-06-30 | 2009-01-27 | Caterpillar Inc. | Regeneration assembly |
US7752850B2 (en) | 2005-07-01 | 2010-07-13 | Siemens Energy, Inc. | Controlled pilot oxidizer for a gas turbine combustor |
US7670135B1 (en) | 2005-07-13 | 2010-03-02 | Zeeco, Inc. | Burner and method for induction of flue gas |
US20070033945A1 (en) * | 2005-08-10 | 2007-02-15 | Goldmeer Jeffrey S | Gas turbine system and method of operation |
US20070044479A1 (en) | 2005-08-10 | 2007-03-01 | Harry Brandt | Hydrogen production from an oxyfuel combustor |
AU2006281992B2 (en) | 2005-08-16 | 2011-05-19 | Kc8 Capture Technologies Ltd | Plant and process for removing carbon dioxide from gas streams |
US7225623B2 (en) | 2005-08-23 | 2007-06-05 | General Electric Company | Trapped vortex cavity afterburner |
EP1757778B1 (de) | 2005-08-23 | 2015-12-23 | Balcke-Dürr GmbH | Abgasführung einer Gasturbine sowie Verfahren zum Vermischen des Abgases der Gasturbine |
US7562519B1 (en) | 2005-09-03 | 2009-07-21 | Florida Turbine Technologies, Inc. | Gas turbine engine with an air cooled bearing |
US7410525B1 (en) | 2005-09-12 | 2008-08-12 | Uop Llc | Mixed matrix membranes incorporating microporous polymers as fillers |
DE102005048911A1 (de) | 2005-10-10 | 2007-04-12 | Behr Gmbh & Co. Kg | Anordnung zur Rückführung und Kühlung von Abgas einer Brennkraftmaschine |
US7690204B2 (en) | 2005-10-12 | 2010-04-06 | Praxair Technology, Inc. | Method of maintaining a fuel Wobbe index in an IGCC installation |
US7513100B2 (en) | 2005-10-24 | 2009-04-07 | General Electric Company | Systems for low emission gas turbine energy generation |
US7493769B2 (en) | 2005-10-25 | 2009-02-24 | General Electric Company | Assembly and method for cooling rear bearing and exhaust frame of gas turbine |
US7827794B1 (en) | 2005-11-04 | 2010-11-09 | Clean Energy Systems, Inc. | Ultra low emissions fast starting power plant |
US8080225B2 (en) | 2005-11-07 | 2011-12-20 | Specialist Process Technologies Limited | Functional fluid and a process for the preparation of the functional fluid |
US7765810B2 (en) | 2005-11-15 | 2010-08-03 | Precision Combustion, Inc. | Method for obtaining ultra-low NOx emissions from gas turbines operating at high turbine inlet temperatures |
EA013360B1 (ru) | 2005-11-18 | 2010-04-30 | Эксонмобил Апстрим Рисерч Компани | Способ добычи углеводородов из подземных пластов (варианты) |
US20070144747A1 (en) | 2005-12-02 | 2007-06-28 | Hce, Llc | Coal bed pretreatment for enhanced carbon dioxide sequestration |
US7726114B2 (en) | 2005-12-07 | 2010-06-01 | General Electric Company | Integrated combustor-heat exchanger and systems for power generation using the same |
WO2007068682A1 (en) | 2005-12-12 | 2007-06-21 | Shell Internationale Research Maatschappij B.V. | Enhanced oil recovery process and a process for the sequestration of carbon dioxide |
US7634915B2 (en) | 2005-12-13 | 2009-12-22 | General Electric Company | Systems and methods for power generation and hydrogen production with carbon dioxide isolation |
AU2006325211B2 (en) | 2005-12-16 | 2010-02-18 | Shell Internationale Research Maatschappij B.V. | Process for cooling down a hot flue gas stream |
US7846401B2 (en) | 2005-12-23 | 2010-12-07 | Exxonmobil Research And Engineering Company | Controlled combustion for regenerative reactors |
US7909898B2 (en) | 2006-02-01 | 2011-03-22 | Air Products And Chemicals, Inc. | Method of treating a gaseous mixture comprising hydrogen and carbon dioxide |
EP1821035A1 (en) | 2006-02-15 | 2007-08-22 | Siemens Aktiengesellschaft | Gas turbine burner and method of mixing fuel and air in a swirling area of a gas turbine burner |
DE102006024778B3 (de) | 2006-03-02 | 2007-07-19 | J. Eberspächer GmbH & Co. KG | Statischer Mischer und Abgasbehandlungseinrichtung |
WO2007102819A1 (en) | 2006-03-07 | 2007-09-13 | Western Oil Sands Usa, Inc. | Processing asphaltene-containing tailings |
US7650744B2 (en) | 2006-03-24 | 2010-01-26 | General Electric Company | Systems and methods of reducing NOx emissions in gas turbine systems and internal combustion engines |
JP4418442B2 (ja) | 2006-03-30 | 2010-02-17 | 三菱重工業株式会社 | ガスタービンの燃焼器及び燃焼制御方法 |
US7591866B2 (en) | 2006-03-31 | 2009-09-22 | Ranendra Bose | Methane gas recovery and usage system for coalmines, municipal land fills and oil refinery distillation tower vent stacks |
US7654320B2 (en) | 2006-04-07 | 2010-02-02 | Occidental Energy Ventures Corp. | System and method for processing a mixture of hydrocarbon and CO2 gas produced from a hydrocarbon reservoir |
US7644573B2 (en) | 2006-04-18 | 2010-01-12 | General Electric Company | Gas turbine inlet conditioning system and method |
US20070249738A1 (en) | 2006-04-25 | 2007-10-25 | Haynes Joel M | Premixed partial oxidation syngas generator |
US20070245736A1 (en) | 2006-04-25 | 2007-10-25 | Eastman Chemical Company | Process for superheated steam |
DE102006019780A1 (de) | 2006-04-28 | 2007-11-08 | Daimlerchrysler Ag | Abgasturbolader in einer Brennkraftmaschine |
WO2007140261A2 (en) | 2006-05-24 | 2007-12-06 | Jupiter Oxygen Corporation | Integrated capture of fossil fuel gas pollutants including co2 with energy recovery |
US7886522B2 (en) | 2006-06-05 | 2011-02-15 | Kammel Refaat | Diesel gas turbine system and related methods |
JP4162016B2 (ja) | 2006-06-08 | 2008-10-08 | トヨタ自動車株式会社 | 内燃機関の排気浄化装置 |
WO2007147216A1 (en) | 2006-06-23 | 2007-12-27 | Bhp Billiton Innovation Pty Ltd | Power generation |
US7691788B2 (en) | 2006-06-26 | 2010-04-06 | Schlumberger Technology Corporation | Compositions and methods of using same in producing heavy oil and bitumen |
US20080006561A1 (en) | 2006-07-05 | 2008-01-10 | Moran Lyle E | Dearomatized asphalt |
MX2008016422A (es) | 2006-07-07 | 2009-01-19 | Shell Int Research | Proceso para producir disulfuro de carbono y uso de una corriente liquida de disulfuro de carbono para la recuperacion mejorada de combustible. |
KR100735841B1 (ko) | 2006-07-31 | 2007-07-06 | 한국과학기술원 | 천연가스 하이드레이트로부터 메탄가스를 회수하는 방법 |
CA2661493C (en) | 2006-08-23 | 2012-04-24 | Praxair Technology, Inc. | Gasification and steam methane reforming integrated polygeneration method and system |
US20080047280A1 (en) | 2006-08-24 | 2008-02-28 | Bhp Billiton Limited | Heat recovery system |
JP4265634B2 (ja) | 2006-09-15 | 2009-05-20 | トヨタ自動車株式会社 | 電動パーキングブレーキシステム |
US7763227B2 (en) | 2006-09-18 | 2010-07-27 | Shell Oil Company | Process for the manufacture of carbon disulphide |
US7520134B2 (en) | 2006-09-29 | 2009-04-21 | General Electric Company | Methods and apparatus for injecting fluids into a turbine engine |
JP2008095541A (ja) | 2006-10-06 | 2008-04-24 | Toufuji Denki Kk | ターボチャージャ |
US7942008B2 (en) | 2006-10-09 | 2011-05-17 | General Electric Company | Method and system for reducing power plant emissions |
US7763163B2 (en) | 2006-10-20 | 2010-07-27 | Saudi Arabian Oil Company | Process for removal of nitrogen and poly-nuclear aromatics from hydrocracker feedstocks |
US7566394B2 (en) | 2006-10-20 | 2009-07-28 | Saudi Arabian Oil Company | Enhanced solvent deasphalting process for heavy hydrocarbon feedstocks utilizing solid adsorbent |
GB0620883D0 (en) | 2006-10-20 | 2006-11-29 | Johnson Matthey Plc | Exhaust system for a lean-burn internal combustion engine |
US7721543B2 (en) | 2006-10-23 | 2010-05-25 | Southwest Research Institute | System and method for cooling a combustion gas charge |
US7492054B2 (en) | 2006-10-24 | 2009-02-17 | Catlin Christopher S | River and tidal power harvester |
US7895822B2 (en) | 2006-11-07 | 2011-03-01 | General Electric Company | Systems and methods for power generation with carbon dioxide isolation |
US7739864B2 (en) | 2006-11-07 | 2010-06-22 | General Electric Company | Systems and methods for power generation with carbon dioxide isolation |
US7827778B2 (en) * | 2006-11-07 | 2010-11-09 | General Electric Company | Power plants that utilize gas turbines for power generation and processes for lowering CO2 emissions |
US7947115B2 (en) | 2006-11-16 | 2011-05-24 | Siemens Energy, Inc. | System and method for generation of high pressure air in an integrated gasification combined cycle system |
US20080118310A1 (en) | 2006-11-20 | 2008-05-22 | Graham Robert G | All-ceramic heat exchangers, systems in which they are used and processes for the use of such systems |
US7921633B2 (en) | 2006-11-21 | 2011-04-12 | Siemens Energy, Inc. | System and method employing direct gasification for power generation |
US20080127632A1 (en) | 2006-11-30 | 2008-06-05 | General Electric Company | Carbon dioxide capture systems and methods |
US7789658B2 (en) | 2006-12-14 | 2010-09-07 | Uop Llc | Fired heater |
US7856829B2 (en) | 2006-12-15 | 2010-12-28 | Praxair Technology, Inc. | Electrical power generation method |
US7815873B2 (en) | 2006-12-15 | 2010-10-19 | Exxonmobil Research And Engineering Company | Controlled combustion for regenerative reactors with mixer/flow distributor |
US7802434B2 (en) * | 2006-12-18 | 2010-09-28 | General Electric Company | Systems and processes for reducing NOx emissions |
EP1944268A1 (en) | 2006-12-18 | 2008-07-16 | BP Alternative Energy Holdings Limited | Process |
US20080155984A1 (en) | 2007-01-03 | 2008-07-03 | Ke Liu | Reforming system for combined cycle plant with partial CO2 capture |
US7943097B2 (en) | 2007-01-09 | 2011-05-17 | Catalytic Solutions, Inc. | Reactor system for reducing NOx emissions from boilers |
US7819951B2 (en) | 2007-01-23 | 2010-10-26 | Air Products And Chemicals, Inc. | Purification of carbon dioxide |
FR2911667B1 (fr) | 2007-01-23 | 2009-10-02 | Snecma Sa | Systeme d'injection de carburant a double injecteur. |
EP2107930B1 (en) | 2007-01-25 | 2012-04-18 | Shell Internationale Research Maatschappij B.V. | Process for reducing carbon dioxide emission in a power plant |
EP1950494A1 (de) | 2007-01-29 | 2008-07-30 | Siemens Aktiengesellschaft | Brennkammer für eine Gasturbine |
US20080178611A1 (en) | 2007-01-30 | 2008-07-31 | Foster Wheeler Usa Corporation | Ecological Liquefied Natural Gas (LNG) Vaporizer System |
US7841186B2 (en) | 2007-01-31 | 2010-11-30 | Power Systems Mfg., Llc | Inlet bleed heat and power augmentation for a gas turbine engine |
US8552073B2 (en) | 2007-02-12 | 2013-10-08 | Sasol Technology (Proprietary) Limited | Co-production of power and hydrocarbons |
EP1959143B1 (en) | 2007-02-13 | 2010-10-20 | Yamada Manufacturing Co., Ltd. | Oil pump pressure control device |
US8356485B2 (en) | 2007-02-27 | 2013-01-22 | Siemens Energy, Inc. | System and method for oxygen separation in an integrated gasification combined cycle system |
US20080251234A1 (en) | 2007-04-16 | 2008-10-16 | Wilson Turbopower, Inc. | Regenerator wheel apparatus |
US20080250795A1 (en) | 2007-04-16 | 2008-10-16 | Conocophillips Company | Air Vaporizer and Its Use in Base-Load LNG Regasification Plant |
US7728736B2 (en) * | 2007-04-27 | 2010-06-01 | Honeywell International Inc. | Combustion instability detection |
CA2587166C (en) | 2007-05-03 | 2008-10-07 | Imperial Oil Resources Limited | An improved process for recovering solvent from asphaltene containing tailings resulting from a separation process |
US8038746B2 (en) | 2007-05-04 | 2011-10-18 | Clark Steve L | Reduced-emission gasification and oxidation of hydrocarbon materials for liquid fuel production |
US7654330B2 (en) | 2007-05-19 | 2010-02-02 | Pioneer Energy, Inc. | Apparatus, methods, and systems for extracting petroleum using a portable coal reformer |
US8616294B2 (en) | 2007-05-20 | 2013-12-31 | Pioneer Energy, Inc. | Systems and methods for generating in-situ carbon dioxide driver gas for use in enhanced oil recovery |
US7918906B2 (en) | 2007-05-20 | 2011-04-05 | Pioneer Energy Inc. | Compact natural gas steam reformer with linear countercurrent heat exchanger |
FR2916363A1 (fr) | 2007-05-23 | 2008-11-28 | Air Liquide | Procede de purification d'un gaz par cpsa a deux paliers de regeneration et unite de purification permettant la mise en oeuvre de ce procede |
BRPI0810590A2 (pt) | 2007-05-25 | 2014-10-21 | Exxonmobil Upstream Res Co | Método in situ de produzir fluidos de hidrocarboneto de uma formação rochosa rica em matéria orgânica |
US7874140B2 (en) | 2007-06-08 | 2011-01-25 | Foster Wheeler North America Corp. | Method of and power plant for generating power by oxyfuel combustion |
US8850789B2 (en) | 2007-06-13 | 2014-10-07 | General Electric Company | Systems and methods for power generation with exhaust gas recirculation |
US20090000762A1 (en) | 2007-06-29 | 2009-01-01 | Wilson Turbopower, Inc. | Brush-seal and matrix for regenerative heat exchanger, and method of adjusting same |
US7708804B2 (en) | 2007-07-11 | 2010-05-04 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Process and apparatus for the separation of a gaseous mixture |
US8061120B2 (en) | 2007-07-30 | 2011-11-22 | Herng Shinn Hwang | Catalytic EGR oxidizer for IC engines and gas turbines |
CA2638588A1 (en) | 2007-08-09 | 2009-02-09 | Tapco International Corporation | Exterior trim pieces with weather stripping and colored protective layer |
CA2697944A1 (en) | 2007-08-30 | 2009-03-05 | Shell Internationale Research Maatschappij B.V. | Process for removal of hydrogen sulphide and carbon dioxide from an acid gas stream |
US7845406B2 (en) | 2007-08-30 | 2010-12-07 | George Nitschke | Enhanced oil recovery system for use with a geopressured-geothermal conversion system |
US8127558B2 (en) | 2007-08-31 | 2012-03-06 | Siemens Energy, Inc. | Gas turbine engine adapted for use in combination with an apparatus for separating a portion of oxygen from compressed air |
US20090056342A1 (en) | 2007-09-04 | 2009-03-05 | General Electric Company | Methods and Systems for Gas Turbine Part-Load Operating Conditions |
US9404418B2 (en) * | 2007-09-28 | 2016-08-02 | General Electric Company | Low emission turbine system and method |
US8167960B2 (en) | 2007-10-22 | 2012-05-01 | Osum Oil Sands Corp. | Method of removing carbon dioxide emissions from in-situ recovery of bitumen and heavy oil |
US7861511B2 (en) * | 2007-10-30 | 2011-01-04 | General Electric Company | System for recirculating the exhaust of a turbomachine |
US8056318B2 (en) * | 2007-11-08 | 2011-11-15 | General Electric Company | System for reducing the sulfur oxides emissions generated by a turbomachine |
CN101939075B (zh) | 2007-11-28 | 2013-08-14 | 布莱阿姆青年大学 | 从废气中捕集二氧化碳 |
US8220268B2 (en) | 2007-11-28 | 2012-07-17 | Caterpillar Inc. | Turbine engine having fuel-cooled air intercooling |
US8133298B2 (en) | 2007-12-06 | 2012-03-13 | Air Products And Chemicals, Inc. | Blast furnace iron production with integrated power generation |
EP2067941A3 (de) | 2007-12-06 | 2013-06-26 | Alstom Technology Ltd | Kombikraftwerk mit Abgasrückführung und CO2-Abscheidung sowie Verfahren zum Betrieb eines solchen Kombikraftwerks |
US8046986B2 (en) | 2007-12-10 | 2011-11-01 | General Electric Company | Method and system for controlling an exhaust gas recirculation system |
US7536252B1 (en) * | 2007-12-10 | 2009-05-19 | General Electric Company | Method and system for controlling a flowrate of a recirculated exhaust gas |
US20090157230A1 (en) | 2007-12-14 | 2009-06-18 | General Electric Company | Method for controlling a flowrate of a recirculated exhaust gas |
JP5118496B2 (ja) | 2008-01-10 | 2013-01-16 | 三菱重工業株式会社 | ガスタービンの排気部の構造およびガスタービン |
GB0800940D0 (en) | 2008-01-18 | 2008-02-27 | Milled Carbon Ltd | Recycling carbon fibre |
US7695703B2 (en) | 2008-02-01 | 2010-04-13 | Siemens Energy, Inc. | High temperature catalyst and process for selective catalytic reduction of NOx in exhaust gases of fossil fuel combustion |
WO2009098597A2 (en) | 2008-02-06 | 2009-08-13 | Osum Oil Sands Corp. | Method of controlling a recovery and upgrading operation in a reservor |
AU2009214660B2 (en) | 2008-02-12 | 2013-01-17 | Foret Plasma Labs, Llc | System, method and apparatus for lean combustion with plasma from an electrical arc |
EP2093403B1 (en) | 2008-02-19 | 2016-09-28 | C.R.F. Società Consortile per Azioni | EGR control system |
US8051638B2 (en) | 2008-02-19 | 2011-11-08 | General Electric Company | Systems and methods for exhaust gas recirculation (EGR) for turbine engines |
US20090223227A1 (en) | 2008-03-05 | 2009-09-10 | General Electric Company | Combustion cap with crown mixing holes |
US8448418B2 (en) | 2008-03-11 | 2013-05-28 | General Electric Company | Method for controlling a flowrate of a recirculated exhaust gas |
US7926292B2 (en) | 2008-03-19 | 2011-04-19 | Gas Technology Institute | Partial oxidation gas turbine cooling |
US8001789B2 (en) | 2008-03-26 | 2011-08-23 | Alstom Technologies Ltd., Llc | Utilizing inlet bleed heat to improve mixing and engine turndown |
US7985399B2 (en) | 2008-03-27 | 2011-07-26 | Praxair Technology, Inc. | Hydrogen production method and facility |
CN104098070B (zh) | 2008-03-28 | 2016-04-13 | 埃克森美孚上游研究公司 | 低排放发电和烃采收系统及方法 |
CN101981272B (zh) | 2008-03-28 | 2014-06-11 | 埃克森美孚上游研究公司 | 低排放发电和烃采收系统及方法 |
EP2107305A1 (en) | 2008-04-01 | 2009-10-07 | Siemens Aktiengesellschaft | Gas turbine system and method |
US8459017B2 (en) | 2008-04-09 | 2013-06-11 | Woodward, Inc. | Low pressure drop mixer for radial mixing of internal combustion engine exhaust flows, combustor incorporating same, and methods of mixing |
US8272777B2 (en) | 2008-04-21 | 2012-09-25 | Heinrich Gillet Gmbh (Tenneco) | Method for mixing an exhaust gas flow |
FR2930594B1 (fr) | 2008-04-29 | 2013-04-26 | Faurecia Sys Echappement | Element d'echappement comportant un moyen statique pour melanger un additif a des gaz d'echappement |
US8240153B2 (en) | 2008-05-14 | 2012-08-14 | General Electric Company | Method and system for controlling a set point for extracting air from a compressor to provide turbine cooling air in a gas turbine |
US8397482B2 (en) * | 2008-05-15 | 2013-03-19 | General Electric Company | Dry 3-way catalytic reduction of gas turbine NOx |
US8209192B2 (en) | 2008-05-20 | 2012-06-26 | Osum Oil Sands Corp. | Method of managing carbon reduction for hydrocarbon producers |
US20090301054A1 (en) | 2008-06-04 | 2009-12-10 | Simpson Stanley F | Turbine system having exhaust gas recirculation and reheat |
US20100003123A1 (en) | 2008-07-01 | 2010-01-07 | Smith Craig F | Inlet air heating system for a gas turbine engine |
US7955403B2 (en) | 2008-07-16 | 2011-06-07 | Kellogg Brown & Root Llc | Systems and methods for producing substitute natural gas |
US20100018218A1 (en) | 2008-07-25 | 2010-01-28 | Riley Horace E | Power plant with emissions recovery |
WO2010014938A2 (en) | 2008-07-31 | 2010-02-04 | Alstom Technology Ltd. | System for hot solids combustion and gasification |
US7674443B1 (en) | 2008-08-18 | 2010-03-09 | Irvin Davis | Zero emission gasification, power generation, carbon oxides management and metallurgical reduction processes, apparatus, systems, and integration thereof |
WO2010020655A1 (en) | 2008-08-21 | 2010-02-25 | Shell Internationale Research Maatschappij B.V. | Improved process for production of elemental iron |
EP2342434B1 (en) | 2008-09-19 | 2012-08-15 | Renault Trucks | Mixing device in an exhaust gas pipe |
US7931888B2 (en) | 2008-09-22 | 2011-04-26 | Praxair Technology, Inc. | Hydrogen production method |
US8316784B2 (en) | 2008-09-26 | 2012-11-27 | Air Products And Chemicals, Inc. | Oxy/fuel combustion system with minimized flue gas recirculation |
US8555796B2 (en) | 2008-09-26 | 2013-10-15 | Air Products And Chemicals, Inc. | Process temperature control in oxy/fuel combustion system |
EA026915B1 (ru) | 2008-10-14 | 2017-05-31 | Эксонмобил Апстрим Рисерч Компани | Способы и системы для регулирования продуктов горения |
US8454350B2 (en) | 2008-10-29 | 2013-06-04 | General Electric Company | Diluent shroud for combustor |
US8015822B2 (en) * | 2008-11-21 | 2011-09-13 | General Electric Company | Method for controlling an exhaust gas recirculation system |
BRPI0920949B1 (pt) | 2008-11-24 | 2020-10-27 | Ares Turbine As | Turbina a gás para transformar energia térmica em trabalho mecânico |
EP2192347B1 (en) | 2008-11-26 | 2014-01-01 | Siemens Aktiengesellschaft | Tubular swirling chamber |
CA2646171A1 (en) | 2008-12-10 | 2010-06-10 | Her Majesty The Queen In Right Of Canada, As Represented By The Minist Of Natural Resources Canada | High pressure direct contact oxy-fired steam generator |
CA2974504C (en) | 2008-12-12 | 2021-04-06 | Maoz Betser-Zilevitch | Steam generation process and system for enhanced oil recovery |
US8112216B2 (en) * | 2009-01-07 | 2012-02-07 | General Electric Company | Late lean injection with adjustable air splits |
US20100170253A1 (en) | 2009-01-07 | 2010-07-08 | General Electric Company | Method and apparatus for fuel injection in a turbine engine |
US8701382B2 (en) * | 2009-01-07 | 2014-04-22 | General Electric Company | Late lean injection with expanded fuel flexibility |
US20100180565A1 (en) * | 2009-01-16 | 2010-07-22 | General Electric Company | Methods for increasing carbon dioxide content in gas turbine exhaust and systems for achieving the same |
JP4746111B2 (ja) | 2009-02-27 | 2011-08-10 | 三菱重工業株式会社 | Co2回収装置及びその方法 |
US20100326084A1 (en) * | 2009-03-04 | 2010-12-30 | Anderson Roger E | Methods of oxy-combustion power generation using low heating value fuel |
US8127937B2 (en) | 2009-03-27 | 2012-03-06 | Uop Llc | High performance cross-linked polybenzoxazole and polybenzothiazole polymer membranes |
US8127936B2 (en) | 2009-03-27 | 2012-03-06 | Uop Llc | High performance cross-linked polybenzoxazole and polybenzothiazole polymer membranes |
US20100300102A1 (en) | 2009-05-28 | 2010-12-02 | General Electric Company | Method and apparatus for air and fuel injection in a turbine |
JP5173941B2 (ja) | 2009-06-04 | 2013-04-03 | 三菱重工業株式会社 | Co2回収装置 |
EA025821B1 (ru) | 2009-06-05 | 2017-02-28 | Эксонмобил Апстрим Рисерч Компани | Топочная система и способы ее применения |
JP5383338B2 (ja) | 2009-06-17 | 2014-01-08 | 三菱重工業株式会社 | Co2回収装置及びco2回収方法 |
US8196395B2 (en) | 2009-06-29 | 2012-06-12 | Lightsail Energy, Inc. | Compressed air energy storage system utilizing two-phase flow to facilitate heat exchange |
US8436489B2 (en) | 2009-06-29 | 2013-05-07 | Lightsail Energy, Inc. | Compressed air energy storage system utilizing two-phase flow to facilitate heat exchange |
EP2284359A1 (en) | 2009-07-08 | 2011-02-16 | Bergen Teknologioverføring AS | Method of enhanced oil recovery from geological reservoirs |
US8348551B2 (en) | 2009-07-29 | 2013-01-08 | Terratherm, Inc. | Method and system for treating contaminated materials |
US8479489B2 (en) | 2009-08-27 | 2013-07-09 | General Electric Company | Turbine exhaust recirculation |
SG10201404506YA (en) | 2009-09-01 | 2014-10-30 | Exxonmobil Upstream Res Co | Low emission power generation and hydrocarbon recovery systems and methods |
US10001272B2 (en) | 2009-09-03 | 2018-06-19 | General Electric Technology Gmbh | Apparatus and method for close coupling of heat recovery steam generators with gas turbines |
US7937948B2 (en) | 2009-09-23 | 2011-05-10 | Pioneer Energy, Inc. | Systems and methods for generating electricity from carbonaceous material with substantially no carbon dioxide emissions |
EP2301650B1 (en) | 2009-09-24 | 2016-11-02 | Haldor Topsøe A/S | Process and catalyst system for scr of nox |
US8381525B2 (en) | 2009-09-30 | 2013-02-26 | General Electric Company | System and method using low emissions gas turbine cycle with partial air separation |
US20110088379A1 (en) | 2009-10-15 | 2011-04-21 | General Electric Company | Exhaust gas diffuser |
US8337139B2 (en) | 2009-11-10 | 2012-12-25 | General Electric Company | Method and system for reducing the impact on the performance of a turbomachine operating an extraction system |
MY158169A (en) | 2009-11-12 | 2016-09-15 | Exxonmobil Upstream Res Co | Low emission power generation and hydrocarbon recovery systems and methods |
IT1396517B1 (it) * | 2009-11-27 | 2012-12-14 | Nuovo Pignone Spa | Metodo di controllo di modo basato su temperatura di scarico per turbina a gas e turbina a gas |
IT1396515B1 (it) * | 2009-11-27 | 2012-12-14 | Nuovo Pignone Spa | Soglia basata su temperatura di scarico per metodo di controllo e turbina |
IT1396516B1 (it) * | 2009-11-27 | 2012-12-14 | Nuovo Pignone Spa | Metodo di controllo di modo basato su temperatura di scarico per turbina a gas e turbina a gas |
US20110126512A1 (en) | 2009-11-30 | 2011-06-02 | Honeywell International Inc. | Turbofan gas turbine engine aerodynamic mixer |
US20110138766A1 (en) | 2009-12-15 | 2011-06-16 | General Electric Company | System and method of improving emission performance of a gas turbine |
US8337613B2 (en) | 2010-01-11 | 2012-12-25 | Bert Zauderer | Slagging coal combustor for cementitious slag production, metal oxide reduction, shale gas and oil recovery, enviromental remediation, emission control and CO2 sequestration |
DE102010009043B4 (de) | 2010-02-23 | 2013-11-07 | Iav Gmbh Ingenieurgesellschaft Auto Und Verkehr | Statischer Mischer für eine Abgasanlage einer Brennkraftmaschine |
US8438852B2 (en) | 2010-04-06 | 2013-05-14 | General Electric Company | Annular ring-manifold quaternary fuel distributor |
US8635875B2 (en) | 2010-04-29 | 2014-01-28 | Pratt & Whitney Canada Corp. | Gas turbine engine exhaust mixer including circumferentially spaced-apart radial rows of tabs extending downstream on the radial walls, crests and troughs |
US8372251B2 (en) | 2010-05-21 | 2013-02-12 | General Electric Company | System for protecting gasifier surfaces from corrosion |
US8627668B2 (en) * | 2010-05-25 | 2014-01-14 | General Electric Company | System for fuel and diluent control |
AU2011271636B2 (en) | 2010-07-02 | 2016-03-17 | Exxonmobil Upstream Research Company | Low emission power generation systems and methods |
CA2801492C (en) * | 2010-07-02 | 2017-09-26 | Exxonmobil Upstream Research Company | Stoichiometric combustion with exhaust gas recirculation and direct contact cooler |
WO2012003077A1 (en) | 2010-07-02 | 2012-01-05 | Exxonmobil Upstream Research Company | Low emission triple-cycle power generation systems and methods |
CN103026031B (zh) * | 2010-07-02 | 2017-02-15 | 埃克森美孚上游研究公司 | 低排放三循环动力产生系统和方法 |
JP5906555B2 (ja) | 2010-07-02 | 2016-04-20 | エクソンモービル アップストリーム リサーチ カンパニー | 排ガス再循環方式によるリッチエアの化学量論的燃焼 |
TWI593878B (zh) | 2010-07-02 | 2017-08-01 | 艾克頌美孚上游研究公司 | 用於控制燃料燃燒之系統及方法 |
US8226912B2 (en) | 2010-07-13 | 2012-07-24 | Air Products And Chemicals, Inc. | Method of treating a gaseous mixture comprising hydrogen, carbon dioxide and hydrogen sulphide |
US8268044B2 (en) | 2010-07-13 | 2012-09-18 | Air Products And Chemicals, Inc. | Separation of a sour syngas stream |
US8206669B2 (en) | 2010-07-27 | 2012-06-26 | Air Products And Chemicals, Inc. | Method and apparatus for treating a sour gas |
US9019108B2 (en) | 2010-08-05 | 2015-04-28 | General Electric Company | Thermal measurement system for fault detection within a power generation system |
US8627643B2 (en) | 2010-08-05 | 2014-01-14 | General Electric Company | System and method for measuring temperature within a turbine system |
US9097182B2 (en) | 2010-08-05 | 2015-08-04 | General Electric Company | Thermal control system for fault detection and mitigation within a power generation system |
WO2012018458A1 (en) | 2010-08-06 | 2012-02-09 | Exxonmobil Upstream Research Company | System and method for exhaust gas extraction |
CN105736150B (zh) | 2010-08-06 | 2018-03-06 | 埃克森美孚上游研究公司 | 优化化学计量燃烧的系统和方法 |
US8220247B2 (en) | 2010-09-13 | 2012-07-17 | Membrane Technology And Research, Inc. | Power generation process with partial recycle of carbon dioxide |
US8166766B2 (en) | 2010-09-23 | 2012-05-01 | General Electric Company | System and method to generate electricity |
US8991187B2 (en) | 2010-10-11 | 2015-03-31 | General Electric Company | Combustor with a lean pre-nozzle fuel injection system |
US8726628B2 (en) | 2010-10-22 | 2014-05-20 | General Electric Company | Combined cycle power plant including a carbon dioxide collection system |
US9074530B2 (en) | 2011-01-13 | 2015-07-07 | General Electric Company | Stoichiometric exhaust gas recirculation and related combustion control |
RU2560099C2 (ru) | 2011-01-31 | 2015-08-20 | Дженерал Электрик Компани | Топливное сопло (варианты) |
TWI563164B (en) * | 2011-03-22 | 2016-12-21 | Exxonmobil Upstream Res Co | Integrated systems incorporating inlet compressor oxidant control apparatus and related methods of generating power |
TWI564474B (zh) * | 2011-03-22 | 2017-01-01 | 艾克頌美孚上游研究公司 | 於渦輪系統中控制化學計量燃燒的整合系統和使用彼之產生動力的方法 |
TW201303143A (zh) | 2011-03-22 | 2013-01-16 | Exxonmobil Upstream Res Co | 低排放渦輪機系統中用於攫取二氧化碳及產生動力的系統與方法 |
TWI593872B (zh) * | 2011-03-22 | 2017-08-01 | 艾克頌美孚上游研究公司 | 整合系統及產生動力之方法 |
TWI563166B (en) * | 2011-03-22 | 2016-12-21 | Exxonmobil Upstream Res Co | Integrated generation systems and methods for generating power |
TWI563165B (en) | 2011-03-22 | 2016-12-21 | Exxonmobil Upstream Res Co | Power generation system and method for generating power |
US20140007590A1 (en) | 2011-03-22 | 2014-01-09 | Richard A. Huntington | Systems and Methods For Carbon Dioxide Capture In Low Emission Turbine Systems |
US8101146B2 (en) | 2011-04-08 | 2012-01-24 | Johnson Matthey Public Limited Company | Catalysts for the reduction of ammonia emission from rich-burn exhaust |
US8910485B2 (en) | 2011-04-15 | 2014-12-16 | General Electric Company | Stoichiometric exhaust gas recirculation combustor with extraction port for cooling air |
US8281596B1 (en) | 2011-05-16 | 2012-10-09 | General Electric Company | Combustor assembly for a turbomachine |
CA2742565C (en) | 2011-06-10 | 2019-04-02 | Imperial Oil Resources Limited | Methods and systems for providing steam |
US8205455B2 (en) | 2011-08-25 | 2012-06-26 | General Electric Company | Power plant and method of operation |
US8453461B2 (en) | 2011-08-25 | 2013-06-04 | General Electric Company | Power plant and method of operation |
US20120023954A1 (en) | 2011-08-25 | 2012-02-02 | General Electric Company | Power plant and method of operation |
US9127598B2 (en) | 2011-08-25 | 2015-09-08 | General Electric Company | Control method for stoichiometric exhaust gas recirculation power plant |
US8713947B2 (en) | 2011-08-25 | 2014-05-06 | General Electric Company | Power plant with gas separation system |
US8266913B2 (en) | 2011-08-25 | 2012-09-18 | General Electric Company | Power plant and method of use |
US8266883B2 (en) | 2011-08-25 | 2012-09-18 | General Electric Company | Power plant start-up method and method of venting the power plant |
US8245492B2 (en) | 2011-08-25 | 2012-08-21 | General Electric Company | Power plant and method of operation |
US8453462B2 (en) | 2011-08-25 | 2013-06-04 | General Electric Company | Method of operating a stoichiometric exhaust gas recirculation power plant |
US8245493B2 (en) | 2011-08-25 | 2012-08-21 | General Electric Company | Power plant and control method |
US8347600B2 (en) | 2011-08-25 | 2013-01-08 | General Electric Company | Power plant and method of operation |
US20130074512A1 (en) * | 2011-09-23 | 2013-03-28 | Steven William Tillery | Inlet fluid flow and impingement angle control |
US20130086917A1 (en) | 2011-10-06 | 2013-04-11 | Ilya Aleksandrovich Slobodyanskiy | Apparatus for head end direct air injection with enhanced mixing capabilities |
EP2581583B1 (en) * | 2011-10-14 | 2016-11-30 | General Electric Technology GmbH | Method for operating a gas turbine and gas turbine |
US9097424B2 (en) | 2012-03-12 | 2015-08-04 | General Electric Company | System for supplying a fuel and working fluid mixture to a combustor |
WO2013147632A1 (en) | 2012-03-29 | 2013-10-03 | General Electric Company | Bi-directional end cover with extraction capability for gas turbine combustor |
JP6002313B2 (ja) | 2012-03-29 | 2016-10-05 | エクソンモービル アップストリーム リサーチ カンパニー | ターボ機械用燃焼器組立体 |
US9353682B2 (en) | 2012-04-12 | 2016-05-31 | General Electric Company | Methods, systems and apparatus relating to combustion turbine power plants with exhaust gas recirculation |
US20130269310A1 (en) | 2012-04-12 | 2013-10-17 | General Electric Company | Systems and apparatus relating to reheat combustion turbine engines with exhaust gas recirculation |
CA2881606C (en) | 2012-04-12 | 2017-07-04 | General Electric Company | System and method for a stoichiometric exhaust gas recirculation gas turbine system |
US20130269361A1 (en) | 2012-04-12 | 2013-10-17 | General Electric Company | Methods relating to reheat combustion turbine engines with exhaust gas recirculation |
US8539749B1 (en) | 2012-04-12 | 2013-09-24 | General Electric Company | Systems and apparatus relating to reheat combustion turbine engines with exhaust gas recirculation |
US20130269357A1 (en) | 2012-04-12 | 2013-10-17 | General Electric Company | Method and system for controlling a secondary flow system |
US20130269358A1 (en) | 2012-04-12 | 2013-10-17 | General Electric Company | Methods, systems and apparatus relating to reheat combustion turbine engines with exhaust gas recirculation |
US20130269356A1 (en) | 2012-04-12 | 2013-10-17 | General Electric Company | Method and system for controlling a stoichiometric egr system on a regenerative reheat system |
US20130269355A1 (en) | 2012-04-12 | 2013-10-17 | General Electric Company | Method and system for controlling an extraction pressure and temperature of a stoichiometric egr system |
US20130269360A1 (en) | 2012-04-12 | 2013-10-17 | General Electric Company | Method and system for controlling a powerplant during low-load operations |
WO2013163045A1 (en) | 2012-04-26 | 2013-10-31 | General Electric Company | System and method of recirculating exhaust gas for use in a plurality of flow paths in a gas turbine engine |
US9784185B2 (en) | 2012-04-26 | 2017-10-10 | General Electric Company | System and method for cooling a gas turbine with an exhaust gas provided by the gas turbine |
US20140208755A1 (en) * | 2013-01-28 | 2014-07-31 | General Electric Company | Gas Turbine Air Mass Flow Measuring System and Methods for Measuring Air Mass Flow in a Gas Turbine Inlet Duct |
US9556798B2 (en) * | 2013-01-28 | 2017-01-31 | General Electric Company | Systems and methods for measuring a flow profile in a turbine engine flow path |
US9938861B2 (en) * | 2013-02-21 | 2018-04-10 | Exxonmobil Upstream Research Company | Fuel combusting method |
-
2011
- 2011-06-09 WO PCT/US2011/039826 patent/WO2012003077A1/en active Application Filing
- 2011-06-09 CA CA2801488A patent/CA2801488C/en not_active Expired - Fee Related
- 2011-06-09 MY MYPI2011002618A patent/MY164051A/en unknown
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- 2011-06-09 SG SG2012087425A patent/SG186084A1/en unknown
- 2011-06-09 EP EP11801317.6A patent/EP2588729B1/en not_active Not-in-force
- 2011-06-09 EA EA201390054A patent/EA029301B1/ru not_active IP Right Cessation
- 2011-06-09 CN CN201710761087.8A patent/CN107575308A/zh active Pending
- 2011-06-09 CN CN201180033204XA patent/CN102985665A/zh active Pending
- 2011-06-09 US US13/702,538 patent/US9903271B2/en active Active
- 2011-06-09 TW TW100120161A patent/TWI564475B/zh not_active IP Right Cessation
- 2011-06-09 BR BR112012031153A patent/BR112012031153A2/pt not_active Application Discontinuation
- 2011-06-09 JP JP2013518420A patent/JP6046612B2/ja not_active Expired - Fee Related
- 2011-06-09 MX MX2012014223A patent/MX352291B/es active IP Right Grant
- 2011-06-29 AR ARP110102287A patent/AR081784A1/es active IP Right Grant
Patent Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB631547A (en) * | 1946-10-04 | 1949-11-04 | Sulzer Ag | Improvements relating to plants in which solid material is subjected to heating and cooling |
CN1142004A (zh) * | 1994-08-05 | 1997-02-05 | Abb管理有限公司 | 空气蓄积器式涡轮机 |
US20020166323A1 (en) * | 2001-03-23 | 2002-11-14 | America Air Liquide, Inc. | Integrated air separation and power generation process |
US20030221409A1 (en) * | 2002-05-29 | 2003-12-04 | Mcgowan Thomas F. | Pollution reduction fuel efficient combustion turbine |
US20080010967A1 (en) * | 2004-08-11 | 2008-01-17 | Timothy Griffin | Method for Generating Energy in an Energy Generating Installation Having a Gas Turbine, and Energy Generating Installation Useful for Carrying Out the Method |
CN1959085A (zh) * | 2005-07-08 | 2007-05-09 | 通用电气公司 | 二氧化碳分离的发电系统和方法 |
CN1996652A (zh) * | 2006-12-28 | 2007-07-11 | 上海交通大学 | 高温燃料电池混合动力协调控制系统 |
US20100115960A1 (en) * | 2007-06-19 | 2010-05-13 | Alstom Technology Ltd | Gas Turbine Installation with Flue Gas Recirculation |
CN101504154A (zh) * | 2008-02-04 | 2009-08-12 | 通用电气公司 | 用于便于组合循环工作流体的改变及其燃烧的方法和系统 |
WO2010072729A2 (en) * | 2008-12-24 | 2010-07-01 | Alstom Technology Ltd | Power plant with co2 capture |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105041506A (zh) * | 2014-06-10 | 2015-11-11 | 摩尔动力(北京)技术股份有限公司 | 内燃闭合循环氢燃料热动力系统 |
CN107864660A (zh) * | 2014-12-31 | 2018-03-30 | 埃克森美孚上游研究公司 | 估计具有排气再循环的燃气涡轮的燃烧当量比的系统和方法 |
CN107849976A (zh) * | 2015-06-15 | 2018-03-27 | 八河流资产有限责任公司 | 用于启动发电设备的系统和方法 |
CN107849976B (zh) * | 2015-06-15 | 2021-11-02 | 八河流资产有限责任公司 | 用于启动发电设备的系统和方法 |
CN106979073A (zh) * | 2015-12-15 | 2017-07-25 | 通用电气公司 | 生成蒸汽且提供冷却的燃烧气体的系统 |
CN106979073B (zh) * | 2015-12-15 | 2020-04-28 | 通用电气公司 | 生成蒸汽且提供冷却的燃烧气体的系统 |
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AU2011271633B2 (en) | 2015-06-11 |
AU2011271633A1 (en) | 2013-01-10 |
CA2801488C (en) | 2018-11-06 |
MY164051A (en) | 2017-11-15 |
TWI564475B (zh) | 2017-01-01 |
SG186084A1 (en) | 2013-01-30 |
EP2588729A1 (en) | 2013-05-08 |
EP2588729A4 (en) | 2017-11-15 |
JP2013533942A (ja) | 2013-08-29 |
EP2588729B1 (en) | 2020-07-15 |
WO2012003077A1 (en) | 2012-01-05 |
CA2801488A1 (en) | 2012-01-05 |
US9903271B2 (en) | 2018-02-27 |
JP6046612B2 (ja) | 2016-12-21 |
US20130104563A1 (en) | 2013-05-02 |
TW201219644A (en) | 2012-05-16 |
EA029301B1 (ru) | 2018-03-30 |
CN107575308A (zh) | 2018-01-12 |
AR081784A1 (es) | 2012-10-17 |
MX2012014223A (es) | 2013-01-18 |
EA201390054A1 (ru) | 2013-04-30 |
BR112012031153A2 (pt) | 2016-11-08 |
MX352291B (es) | 2017-11-16 |
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