CN101981272B - 低排放发电和烃采收系统及方法 - Google Patents

低排放发电和烃采收系统及方法 Download PDF

Info

Publication number
CN101981272B
CN101981272B CN200980111019.0A CN200980111019A CN101981272B CN 101981272 B CN101981272 B CN 101981272B CN 200980111019 A CN200980111019 A CN 200980111019A CN 101981272 B CN101981272 B CN 101981272B
Authority
CN
China
Prior art keywords
stream
carbon dioxide
hydrocarbon
gaseous state
gaseous
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN200980111019.0A
Other languages
English (en)
Other versions
CN101981272A (zh
Inventor
M·明特
F·F·米特里克尔
P·C·拉斯马森
L·K·斯塔尔切尔
C·C·拉斯马森
J·T·威尔金斯
R·W·迈德尔
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ExxonMobil Upstream Research Co
Original Assignee
Exxon Production Research Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Exxon Production Research Co filed Critical Exxon Production Research Co
Publication of CN101981272A publication Critical patent/CN101981272A/zh
Application granted granted Critical
Publication of CN101981272B publication Critical patent/CN101981272B/zh
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
    • F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
    • F01K23/06—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
    • F01K23/067—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle the combustion heat coming from a gasification or pyrolysis process, e.g. coal gasification
    • F01K23/068—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle the combustion heat coming from a gasification or pyrolysis process, e.g. coal gasification in combination with an oxygen producing plant, e.g. an air separation plant
    • E—FIXED CONSTRUCTIONS
    • E21—EARTH DRILLING; MINING
    • E21B—EARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
    • E21B43/164—Injecting CO2 or carbonated water
    • E—FIXED CONSTRUCTIONS
    • E21—EARTH DRILLING; MINING
    • E21B—EARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
    • E21B43/18—Repressuring or vacuum methods
    • E—FIXED CONSTRUCTIONS
    • E21—EARTH DRILLING; MINING
    • E21B—EARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/34—Arrangements for separating materials produced by the well
    • E21B43/40—Separation associated with re-injection of separated materials
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
    • F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
    • F01K23/06—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
    • F01K23/10—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle with exhaust fluid of one cycle heating the fluid in another cycle
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00—Capture or disposal of greenhouse gases
    • Y02C20/40—Capture or disposal of greenhouse gases of CO2
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/14—Combined heat and power generation [CHP]
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
    • Y02E20/18—Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P90/00—Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
    • Y02P90/70—Combining sequestration of CO2 and exploitation of hydrocarbons by injecting CO2 or carbonated water in oil wells

Abstract

提供了在烃采收方法中低排放发电的方法和系统。一个系统包括低排放发电的集成的压力保持和混相驱动系统。可选的系统提供了使用热气体膨胀器和外部燃烧器的低排放发电、碳分离、提高采收率法采油(EOR)或二氧化碳出售。另一可选的系统提供了使用气体发电轮机以在入口压缩机中压缩空气并使用膨胀器内的热二氧化碳充载气体发电的低排放发电。通过合并热交叉交换、脱盐设备、共生产和其它特征可以获得其它功效。

Description

低排放发电和烃采收系统及方法
交叉引用相关申请
本申请要求2008年3月28日提交的美国临时申请号61/072,292和2009年2月18日提交的美国临时申请号61/153,508的权益。
发明领域
本发明的实施方式涉及烃采收方法中的低排放发电。更具体而言，本发明的实施方式涉及利用氮、氧、二氧化碳和烃燃料在极低排放的烃采收方法中发电的方法和装置。
发明背景
本节意图介绍与本发明的示例性实施方式相关的本领域的各个方面。相信该讨论有助于提供一个基本概念，以利于更好地理解本发明的特定方面。因此，应该理解，本节应该基于此进行阅读，并不必承认其为现有技术。
多种强化烃采收操作可以被分类为以下类型之一：压力保持和混相驱动(miscible flooding)。在压力保持操作中，惰性气体如氮被注入主要为气态的油藏，以在该油藏内至少保持最低压力，阻止反凝析并提高总采收量。在混相驱动操作中，混相气体如二氧化碳被注入主要为液态的油藏以与液体混合，降低其粘度并增加压力以提高采收率。
许多产油国正在经历强烈的国内电力需求增长，并关注于提高采收率法采油(EOR)，以提高从其油藏采油。两种常见的EOR技术包括用于油藏压力保持的氮气(N2)注入和用于EOR混相驱动的二氧化碳(CO2)注入。还有全球关注的温室气体(GHG)排放问题。这种关注与许多国家的总量控制与交易政策(cap-and-trade)的执行相结合，使得减少CO2排放成为这些和其它国家以及其中操作烃生产系统的公司优先考虑的事情。
减少CO2排放的一些方法包括燃料脱碳或燃烧后捕集。但是，这两种方法成本都高并且降低发电效率，导致电力生产量降低，为满足国内电力需求而增加了燃料的需求并增加了电的成本。另一种方法是联合循环方式(in a combined cycle)的含氧燃料燃气轮机(例如，来自燃气轮机Brayton循环的废热被捕集以在Rankin循环中产生蒸汽并产生额外电力)。然而，没有商业可得的燃气轮机能够在这样的循环内进行操作，并且产生高纯氧所需的电力显著降低了该方法的总效率。一些研究比较了这些方法并显示了每种方法的一些优势。参见例如BOLLAND、OLAV和UNDRUM，HENRIETTE，Removal of CO2 fromGas Turbine Power Plants：Evaluation of pre-and post-combustionmethods，SINTEF Group，参见http://www.energy.sintef.no/publ/xergi/98/3/3art-8-engelsk.htm(1998)。
美国专利号4,344,486(′486专利)公开了一种方法，所述方法是向采出的烃和来自产液地层的二氧化碳中添加基本纯的氧以产生热或电，并再次注入二氧化碳用于EOR。所述′486专利公开，将烃液体与产液地层的采出液流中的气态组分分离，然后将所述气态组分与基本纯的氧混合并燃烧所述混合物以产生热和CO2。然后CO2被注入相同或不同的产液地层。该方法没有教导或建议解决制氧厂效率低下(efficiency drag)问题的方案。
美国专利公开号2007/0237696(′696出版物)基本上公开了含氧燃料方法和′486专利中公开的EOR的组合。′696出版物也要求独立的制氧厂或空气分离厂，没有教导或建议工作气体发电轮机配置。
因此，仍然十分需要低排放、高效率的烃采收方法。
发明概述
本发明的一个实施方式公开了集成系统。所述集成系统包括空气分离机构其被配置为产生高纯氧流和高纯氮流；气态控制燃料流；燃烧机构，其被配置为使至少所述气态控制燃料流和所述高纯氧流燃烧以产生含二氧化碳和水的气态燃烧流；发电系统，其被配置为接收所述含二氧化碳和水的气态燃烧流并至少产生压缩的、气态的、基本为二氧化碳的流；第一注入器机构，其被配置为将所述压缩的、气态的、基本为二氧化碳的流的至少一部分注入提高采收率法采油油藏；和第二注入器机构，其被配置为将所述高纯氮流的至少一部分注入压力保持油藏。在一个实施方式中，所述发电系统包括膨胀器，其被配置为接收所述气态燃烧流并产生至少一个单位的机械能和气态排出流；热回收机构，其被配置为接收并冷却所述气态排出流，产生至少一个单位的热能，并生成至少一体积的水和冷却的、气态的、基本上为二氧化碳的流，其中所述热能被任选地用于产生蒸汽以产生蒸汽能；和二氧化碳压缩机，其被配置为压缩所述冷却的、气态的、基本上为二氧化碳的流以产生所述压缩的、气态的、基本为二氧化碳的流。所述系统还可以包括第一烃采收油藏，其被配置为产生第一烃混合物；和第一烃分离机构，其被配置为至少将液体烃从所述第一烃混合物中分离出来并产生第一烃流和包括二氧化碳的第二气体流，其中所述燃烧机构被进一步配置为利用所述第二气体流的至少一部分与所述气态控制燃料流和所述高纯氧流，产生所述含二氧化碳和水的气态燃烧流。所述系统可以进一步包括第二烃采收油藏，其被配置为产生第二烃混合物；和第二烃分离机构，其被配置为至少将液体烃从所述第二烃混合物中分离出来并产生第二烃流和包括氮气的惰性气体流，其中所述第二注入器进一步被配置以将所述惰性气体流注入所述压力保持油藏。
本发明的另一实施方式公开了改进的烃采收方法。所述方法包括将空气分离成高纯氧流和高纯氮流；提供气态控制燃料流；在燃烧器内燃烧至少所述气态控制燃料流和所述高纯氧流以形成含二氧化碳和水的气态燃烧流；将所述含二氧化碳和水的气态燃烧流接收入发电系统，其中所述发电系统至少产生压缩的、气态的、基本上为二氧化碳的流；将所述压缩的、气态的、基本上为二氧化碳的流的至少一部分注入提高采收率法采油油藏；以及将所述高纯氮流的至少一部分注入压力保持油藏。
在本发明的第三个实施方式中，公开了低排放发电系统。所述系统包括第一烃采收油藏，其被配置为产生第一烃混合物；第一烃分离机构，其被配置为至少将液体烃从所述第一烃混合物中分离出来并产生第一烃流和包括二氧化碳的第二气体流；气态控制燃料流；高纯氧流；外部燃烧器，其被配置为使所述气态控制燃料流、所述高纯氧流和所述包含二氧化碳的第二气体流的组合燃烧，以产生气态燃烧流；热气体膨胀器，其被配置为接收所述气态燃烧流并产生至少一个单位的机械能和至少具有二氧化碳组分和水组分的气态排出流；和操作系统，其被配置为调节所述气态排出流以从中充分地除去所述水组分并利用所述二氧化碳组分的至少一部分。
在本发明的第四个实施方式中，提供了低排放发电的方法。所述方法包括从第一烃采收油藏产生第一烃混合物；将所述第一烃混合物分离为第一烃流和包括二氧化碳的第二气体流；提供高纯氧流；提供气态控制燃料流；在外部燃烧器内使至少所述高纯氧流和所述气态控制燃料流的组合燃烧，以产生含二氧化碳和水的气态燃烧流；使所述气态燃烧流在热气体膨胀器内膨胀以产生至少一个单位的机械能和具有水组分和二氧化碳组分的气态排出流；从所述气态排出流中除去所述水组分的至少一部分；和利用所述排出(尾气)流的二氧化碳组分的至少一部分。
在本发明的第五个实施方式中，公开了低排放发电系统。所述系统包括第一烃采收油藏，其被配置为产生第一烃混合物；第一烃分离机构，其被配置为至少将液体烃从所述液体烃混合物中分离出来并产生第一烃流和包括二氧化碳的第二气体流；气态控制燃料流；空气分离机构，其被配置为至少提供高纯氧流；燃烧器，其被配置为使所述气态控制燃料流、所述高纯氧流和包含二氧化碳的所述第二气体流的组合燃烧以产生气态燃烧流；和气体发电轮机。所述气体发电轮机包括：入口压缩机，其中所述入口压缩机被配置为压缩大气以送至所述空气分离机构；和膨胀器，其被配置为接收所述气态燃烧流并产生至少一个单位的机械能和至少具有二氧化碳组分和水组分的气态排出流。所述发电系统进一步包括操作系统，其被配置为调节所述气态排出流以充分地除去所述气态排出流的水组分并利用所述气态排出流的二氧化碳组分的至少一部分。
在本发明的第六个实施方式中，提供了低排放发电的方法。所述方法包括从第一烃采收油藏产生第一烃混合物；将所述第一烃混合物分离为第一烃流和包括二氧化碳的第二气体流；在空气分离机构内分离空气，所述空气分离机构被配置以至少产生高纯氧流；提供气态控制燃料流；在燃烧器内使至少所述高纯氧流和所述气态控制燃料流的组合燃烧，以产生含二氧化碳和水的气态燃烧流；在气体发电轮机的入口压缩机内压缩空气以形成压缩的空气流；将所述压缩的空气流提供至所述空气分离机构；使所述气态燃烧流在所述气体发电轮机的膨胀器内膨胀，以产生至少一个单位的机械能和至少具有水组分和二氧化碳组分的气态排出流；从所述气态排出流中除去所述水组分的至少一部分；和利用所述二氧化碳组分的至少一部分。
附图简述
研读以下详细说明和实施方式的非限制性实例的附图后，本发明的前述和其它优势将变得明显，附图中：
图1A-1B图解了本发明的用于低排放发电和烃采收的集成系统；
图2图解了示例性燃烧器的示意图，其可以被配置用于图1A-1B的系统中；
图3是操作图1A-1B系统的方法的示例性流程图；
图4图解图1A-1B的低排放发电系统的另一实施方式；
图5是操作图4的系统的方法的示例性流程图；
图6图解图1A-1B的低排放发电系统的又一实施方式；和
图7是操作图6的系统的方法的示例性流程图；
图8A-8C图解图1A-1B的低排放发电系统的另外的可选实施方式。
发明详述
在以下发明详述部分，结合优选的实施方式描述本发明的具体实施方式。但是，就以下描述特定于本发明的具体实施方式或具体使用而言，这意图仅为示例性的目的并仅仅提供示例性实施方式的描述。因此，本发明并不限于以下所描述的具体实施方式，而是，其包括落入所附权利要求的精神和范围内的所有可选项、改型和等同物。
本系统的至少一个益处是集成两种采收方法以产生两种注入气体(氮和CO2)用于另外的烃采收。为实现这一点，首先压缩空气。可以捕集压缩期间产生的热量并用于发电或盐水脱盐。然后冷却的压缩空气被送至空气分离机构(ASU)。ASU产生氮流和氧流。氧与燃料气体和CO2结合并用于烃的燃烧。然后燃烧产物被送至膨胀器以产生动力，所述膨胀器可以是热气体膨胀器或气体发电轮机的膨胀器(其可以在与发电机整合的轴上或驱动分离发电机的整合轴上)。然后来自膨胀器的排出气体被用于加热移向燃烧器的CO2以提高循环效率、产生可用于产生另外能量或盐水脱盐的蒸汽，或者既用于加热移向燃烧器的CO2，增加效率，又用于提供能量和/或脱盐。然后燃烧产物(CO2和水)被进一步冷却以使水冷凝并产生CO2流，所述CO2流可以在系统内循环，任选地与所述氧流预混合以稀释，被分离，用于提高采收率法采油(EOR)，或出售给第三方。
本公开系统和方法的实施方式可以被用于产生超低排放电力和用于EOR的CO2。通过在动力装置循环中将通常循环返回的CO2用于另外的EOR，可以产生电力，向大气排放很少或没有排放NOx或CO2。来自常规EOR采收系统的CO2和轻烃被压缩并与氧和其它燃料气体一起燃烧，然后在热气体膨胀器内膨胀以产生电力。也可以通过在冷凝蒸汽循环如热回收蒸汽发生器(HRSG)中对来自热气体膨胀器的排出气体进行热回收来产生额外的电力。因为化学计量燃烧的产物仅仅是CO2和水，可以通过冷却烟道气和从流中冷凝出水来产生高纯CO2流。该方法的结果是产生电力并生产额外的CO2。然后所述CO2流(在一些实施方式中减去再循环组分)被送回EOR设备进行另外的压缩并再注入返回井中，用于另外的采油。
尽管完全独立地生产用于油藏压力保持的氮和用于EOR的二氧化碳是可能的，但是本公开系统和方法的实施方式利用了这样的协同作用——当以集成方法产生氮和二氧化碳以低得多的成本产生这些气体同时也产生电力和/或超低排放的脱盐水时这是可能。值得注意的是，如果EOR利用是不可能的，则通过发电产生的CO2可以从再循环流中被清除并被分离或储存。这允许各种实施方式被用于以超低排放发电。
在典型的气井压力增强或保持操作中，一般通过从空气中分离氮(例如在ASU中)来产生氮以达到注入井要求的氮流的规格。这样的方法产生富氧流，其被排回到大气中。通过给ASU增加相对小量的递增动力和投资，空气可以被分离成高纯氮流和高纯氧流。为产生廉价的CO2，高纯氧流是期望的。如果在大量氮的存在下发生燃烧，那么将需要昂贵的和能量密集型加工设备将CO2从其它气体如一氧化二氮(NOx)中分离出来。本发明目前公开的许多实施方式使用高纯氧流来燃烧烃并产生CO2和水。通过简单地冷却燃烧产物来完成水的分离。
在一个示例性实施方式中，高纯氧流可以被用于产生廉价的CO2和水。较低纯度的氧具有两个问题。第一，基于低纯氧的燃烧产物分离相对昂贵——极端的是基于空气作为氧化剂的燃烧产物。这可以导致过于昂贵的烟道气分离。第二，所得到的烟道气的较低热容降低了所公开实施方式的总热力学优势。最大化工程经济所需的氧纯度水平因工程的不同而不同。一般而言，所需的纯度水平可以不低于50％。这用空气分离方法如基于膜或低温方法的分离方法可以达到。特别地，本公开系统的一个实施方式利用基于低温分离的空气分离机构(ASU)或利用分子筛的分离。在用于基于低温的ASU的氧纯度谱的低端是对于高纯氮生产优化的ASU设计，这使氧纯度低于70％。该流可以包含大于20％的氮水平。在所述谱的另一端是对于高纯氧生产优化的ASU设计，其中甚至氩也被从氧中分离出来，这使得氧纯度接近于100％。
在本公开的一些实施方式中，ASU是用于从空气中分离氮和氧的低温方法。与ASU相关的成本依赖于所期望的产品纯度。相较于生产95％氧，生产99.5％纯氧要求明显增加的资金和马力。因此，在含氧燃料燃烧中使用的氧的纯度应该基于燃烧产物的规格而进行限定。如果要求高纯CO2流，那么可能需要高纯氧。如果燃烧产物被排出，那么可以使用较低纯度的氧。
在一个实施方式中，燃烧在升高的压力下进行，所以通过使燃烧产物膨胀穿过膨胀器，可以产生额外的电力。Brayton循环的效率是跨膨胀器的压力比率和膨胀器的入口温度的函数。因此，使压力比率增高和膨胀器入口温度增高增加燃气轮机的效率。膨胀器的入口温度可以由材料事项和部件表面的冷却限制。在一些实例中，储层气体具有高井口压力(例如，从约1,000磅每平方英寸(psi)至约6,000psi)和高浓度的惰性气体，所以可以不需要增压器。在高压燃烧器使用这些类型的燃料然后在膨胀器部分使之膨胀可以产生高效率并提供利用这些储层的经济方式。依据可获得的井口压力，在升高的压力下也可以停止膨胀以减少与压缩用于EOR的CO2或分离CO2相关的成本。例如，使膨胀器排气为1barg(1bar表压或约14.5psig)相较于仅有几英寸水的正压可以节省几乎25％的使CO2获得临界条件(在临界点或高于临界点——约31℃和约73.8barg或1,070psig)所需的压缩能。将膨胀器背压增加至5barg(约72.5psig)节约大约55％的压缩能，将背压增加至10barg(约145psig)节约大约70％的CO2压缩能。
使用的燃烧器可以类似于在气化方法中使用的那些，其中氧和烃在还原气氛(reducing atmosphere)下反应，使用蒸汽调节温度。在本发明中，CO2将代替蒸汽使用以调节温度。使用蒸汽是昂贵的并会导致在燃烧产物中形成额外的氢，这在本循环中是不期望的。通过将CO2与氧混合，有可能使用更多传统的扩散型燃烧器——类似于在现有燃气轮机中使用的那些，其中CO2将代替空气使用以冷却燃烧衬里。优选接近化学计量条件下的燃烧(或″稍微富余″的燃烧)以消除除去额外氧的成本。如果火焰稳定性要求较稀浓度燃烧(leaner combustion)，除去氧的商业技术目前是可获得的。
现在参考附图，图1A-1B图解了用于本发明低排放发电和烃采收的集成系统。在图1A中，系统100包括空气分离机构124和气态控制燃料流125，空气分离机构124从大气流123中产生高纯氧流128和高纯氮流126。也提供燃烧器134，其至少燃烧氧流128和燃料流125的组合，以产生气态燃烧流136。发电系统139接收燃烧流136并生成水155、电140和压缩的、气态的、基本为二氧化碳的流162，其被送至注入压缩机164以形成注入流166，用于注入提高采收率法采油油藏或二氧化碳分离位置167。氮流126被送至注入压缩机169以形成注入流170，用于注入压力保持油藏或氮气储存位置171。
图1B图解系统100的示例性实施方式。系统101包括产生第一混合流体烃采出流103的第一烃采收油藏102，并包括分离机构104、液体烃产物流106、包括一些二氧化碳(CO2)和轻烃(例如甲烷、乙烷等)的第二气态原料流108——其可以与再循环流160混合以形成包含基本是CO2(例如从约60体积百分比至约95vol％)的低能量(例如低BTU)流109、至少一个压缩机构110A-110X——其包括压缩机并可以包括冷却机构以压缩和冷却低能量流109来提供第一压缩低能量气态流112。系统100进一步包括产生第二混合流体烃采出流114的第二烃采收油藏113、第二分离机构116、烃产物流118和包含基本是氮(N2)(例如从约70体积百分比至约100vol％)的惰性气体原料流120。系统100还包括空气进入流121，其在压缩机122中被压缩以形成压缩空气进入流123，其进入空气分离机构124以产生高纯氮流(例如从约85vol％至约100vol％)126和高纯氧流(例如从约70vol％至约100vol％)128。高纯氧流128在燃烧器134内与气态控制燃料流125一起燃烧。低能量气态流112也被引入燃烧器134用于温度控制、质量流并可能用于流112中部分烃的部分燃烧。
高纯氧流128与气态控制燃料流125在燃烧器134内的组合被配置为保持最低绝热火焰温度和火焰稳定性，以燃烧富氧燃料流128中的所有或几乎所有的氧(例如，优选为化学计量反应)。就热值而言，氧流128没有热值，控制燃料流125具有相对大的热值(例如从至少300英国热单位每标准立方英尺(BTU/scf)至约900BTU/scf或从约500BTU/scf至约700BTU/scf)，低能量流112具有相对小的热值(例如从约100BTU/scf至约450BTU/scf或从约150BTU/scf至约300BTU/scf)。值得注意的是，当控制燃料流125与低能量流112预先混合时，混合流的热值可以是从约200BTU/scf至约500BTU/scf。流112、125和128的燃烧产生气态燃烧流136，其可以与低能量气体侧流112′混合以提供冷却，形成膨胀器进入流137，流137进入膨胀器138以产生机械能140和气态排出流142。要注意的是，膨胀器138可以是动力燃气轮机上的膨胀器或热气体膨胀器。
气态排出流142基本上可以包括二氧化碳和蒸发的水，并被送至热回收蒸汽发生器(HRSG)144或类似装置。HRSG 144产生蒸汽流146，其可以被送至蒸汽轮机150以产生额外的能量152，冷却的排出气体148被送至冷却机构154，其产生水排空流155和基本上为二氧化碳的流156。基本上为二氧化碳的流156被送至配置为形成压缩的二氧化碳流162的压缩机158，流162被送至井注入压缩机164，于此流162被压缩以形成高度压缩的二氧化碳流166，用于注入提高采收率法采油(EOR)油藏167。同时，惰性气体原料流120可以与高纯氮流126混合以形成压力保持流168，其可以在压缩机169内被压缩以形成注入流170，用于注入压力保持油藏或氮储库171。
尽管提及四个油藏101、113、167和171，但油藏可以都是同一个油藏，是两个、三个或四个不同的油藏，并可以包括多个用于注入或生产的油藏。此外，采出流102和114的内含物可能随时间改变，特别是在注入气体开始生成的“突破点”。
一般而言，EOR油藏167是包含基本上是液体烃如原油的油藏或其一部分并且通常位于含水层之上。液体烃在适当的温度和压力下与注入的压缩二氧化碳流166可混相。高CO2浓度(例如上至约90体积％或以上)以这样的混相驱动操作是优选的，因为CO2用作稀释剂以降低油的粘度和作为溶剂以从地层岩石中除去油以及其它原因。此外，如果混合适当，将气体166泵入油藏需要更少的动力。注入流166中的氧水平优选地保持非常低。
一般而言，压力保持油藏171是在产油层上包括气顶的油藏或其一部分。当产生液体时，气顶压力和地层压力减少，导致较低的生产力并且可能在气体部分导致反缩合。注入气体170被配置为保持油藏内的压力以至少保持采收压力并避免反缩合。混相能力不是这种操作中的问题。因此，惰性气体如氮是优选的。在至少注入油藏167和171是同一个的具体示例性情况中，氮可以被注入油藏的气顶，二氧化碳被用作混相注入物，以在同一油藏中用于EOR。
采出流103和114可以是相同的或不同的，或者包括来自多个油藏的生产并且可以包括任何种类的轻或重液体和气态烃组分以及其它非烃组分如二氧化碳、硫化氢、氮、硫化羰及其组合。在最初或早期阶段的生产期间，预期在采出流103和114中具有比酸或非烃组分明显多的重烃组分。新鲜的(sweet)流103和114的示例性内含物包含从至少约70摩尔百分比(mol％)的烃至约99mol％烃、从约1mol％至约5mol％CO2、从约0mol％N2至约5mol％N2以及一些其它组分。
在烃被采出时以及特别地一旦气体发生冲出，组成可以发生急剧变化。例如，在CO2冲出之后，示例性采出流103或114可以具有以下含量：约5摩尔百分比(mol％)的烃至约60mol％的烃，从约40mol％至约95mol％的CO2，从约0mol％N2至约10mol％N2以及一些其它组分。在氮冲出之后，示例性采出流103或114可以具有以下含量：约5摩尔百分比(mol％)的烃至约60mol％的烃，从约5mol％至约20mol％的CO2，从约40mol％的N2至约95mol％N2以及一些其它组分。要注意的是，冲出是个瞬时过程而不是逐步过程，逐步过程相对快但产生的气体冲出量逐步增加。例如，油藏在早期生产期间可以稳定地产生约5mol％的CO2，然后在过渡期(从一个月到几年)产生渐增量的CO2，直至CO2的产生达到约95mol％CO2的高稳态产生。
分离机构104和116可以是相同的机构、不同的机构、或每个包含多个机构，这些多个机构取决于采出流103和114的内容物而分别串联或并联。分离机构104和116可以包含用于烃分离的任何已知的技术，如例如：冷冻、解吸油吸附、在固体吸附剂如硅胶上吸附、吸附动力学分离、低温分离或这些方法的一些组合。进一步地，一旦发生冲出，分离组分、设备和方法可能要求调整、去瓶颈或总替换以应对采出流内含物的差异。
第一和第二烃产物流106和118可以包含轻烃和重烃，如丙烷、丁烷、戊烷、己烷或芳香烃、天然汽油以及甚至原油。产物流106和118优选地被送至下游用于进一步处理，和出售或其它应用，但流106′和118′的一部分可以被用在系统100中。在分离之后，剩余的气态流108和120将分别具有采出流103和114的内含物，但较重的烃被分离机构104和116除去。
下表提供系统100的实施方式中气态流112、125、128、136、137和162的示例性组成(以及引入流112、125和128的摩尔流量比率)，其中基本上是二氧化碳的流156被注入提高采收率法采油操作中的烃采收油藏并且是在CO2冲出之后。流112、125和128的流量比率是按体积分数。
表1
Figure BPA00001231657000121
在初始气态流103或108处于足够高压力下的一些实施方式中，可以不需要压缩机110A-110X。在其它实施方式中，压缩机110A-110X可以包括一至四个离心压缩机110A-110D，在其之间可以包括中间冷却器，根据系统要求和经济学，还可以有单个轴向压缩机110或一些组合。如所述，燃烧器134和膨胀器138内的较高压力可以提高系统101的总效率。例如，膨胀器排气142可以从约1barg至约10barg或约4barg至约6barg或约5barg。预期的是，本领域普通技术人员具有足够的信息来设计压缩机110A-110X、燃烧器134和膨胀器134，以获得根据本公开的较高压力膨胀器排气。
在另外的实施方式中，使流112保持较高温度用于混合以及在燃烧器134内进行燃烧可以是期望的。可以通过与热排出气体流136或142(如果使用流142，可以在交叉交换之间将其压缩)、系统100内其它压缩机(例如压缩机122、压缩机158或压缩机164)中的一个产生的热或HRSG144的交叉交换来加热流112。优选的是足以提高燃烧器134内燃烧效率的温度。在一个实施方式中，酸性气体流112在进入燃烧器134时可以为约50摄氏度(℃)至约500℃。
燃烧器134可以是标准的外部燃烧器或可以是定制的或改进的燃烧器。可使用的燃烧器类型的实例包括oxyClaus燃烧器、部分氧化(POX)燃烧器、自热重整(ATR)燃烧器、扩散燃烧器(diffusion burners)、贫燃预混(lean-premix)燃烧器和点火燃烧器。要注意的是，每个燃烧器类型可以要求一些改进以与基本上是CO2的流一起工作。在扩散火焰燃烧器(或″燃烧装置″)中，燃料与氧化剂混合并同时在主燃烧区燃烧。扩散燃烧器产生接近化学计量的燃料/空气混合物区域，在此区域，温度非常高。在预混合燃烧器中，燃料和空气在初始阶段被完全混合，形成均匀、贫燃、未燃烧的燃料/空气混合物，其被送至发生燃烧反应的第二阶段。目前贫燃预混燃烧器因为较低的火焰温度在燃气轮机中常用，其产生较低的NOx排放。在点火燃烧器中，热点火引导确保在其周围的贫燃料氧化剂混合物保持稳定燃烧。这些点火燃烧器通常被用于航空发动机和用于其本身不能保持稳定燃烧的燃料。
图2图解了示例性燃烧器134的示意图，其可被配置用于系统100中。因此，可以参考图1A-1B最好地理解图2。燃烧器134的该实施方式可以被称作″氧燃烧器″并包括燃烧室200、气体混合室(或喷雾室)202、燃烧喷嘴206、第二气体入口204A-204B和外壁(或护罩)210。
在一个示例性实施方式中，喷雾室202以及喷嘴204A-204B和206可以被配置为以高度激烈的方式使天然气流125与包含酸性气体流112和高纯氧流128的氧化流混合，以确保获得均匀的混合物。在操作期间，火焰208产生上至约2,200℃的温度。随着冷却气体112的加入，排出气体212预期上至约1,400℃。可以经外壁210引入额外的冷却气体112，产生一种″气体包围层(gas envelope)″以使室200的璧比火焰208明显冷。在一个示例性实施方式中，如果需要，冷却流112可以被除去烃以最小化煤烟的形成。在另一示例性实施方式中，在高于大气压的压力下发生燃烧。反应生成水(蒸汽)和二氧化碳，如以下方程式所示(进入室内的二氧化碳通常保持未反应)：
CH4+2O2＝2H2O+CO2
燃烧过程的特征在于高的燃料对氧化剂之比，其远超过化学计量比，导致过于充足的燃烧过程。可以通过精确计量进入燃烧器134的氧128和天然气125来实现燃烧反应的控制。温度也被用于修正燃料和氧流量的控制。在包括EOR的优选实施方式中，燃料125和氧128被计量以产生恰低于化学计量的混合物，优选地在富余氧一侧，以避免在得到的流136中有尽量多的氧。基于燃烧产物的反馈控制可以被用于修正燃料和氧之比。
典型的部分氧化(POX)燃烧器将天然气125与蒸汽氧化流146混合成均匀的混合物。蒸汽的添加不仅用来调节反应温度还在反应中产生额外的氢。部分氧化过程的特征在于高的燃料对氧化剂之比，远超过化学计量比。POX是超富燃烧过程的实例。
典型的oxyClaus燃烧器(未显示)包括围绕中心起始燃烧器马弗炉的多个酸性气体燃烧器。每个酸性气体燃烧器包括来自氧流128、低能量流112和控制燃料流125的原料或“喷入”。温度可以上至约2,200℃(约1,900K)或者甚至更高。组合的原料流128、112和125可以形成非常热的氧火焰，其被如来自控制流112′的更冷的气体包围层包围。
在典型的热自热重整(ATR)方法(未显示)中，天然气-蒸汽(例如125和146)和氧128的混合物被送人燃烧器134。在燃烧区发生部分氧化反应，然后产物通过催化剂床，在此发生重整反应。ATR反应器由带有燃烧器、燃烧室和催化剂床的耐火衬里压力容器组成。其设计类似于POX反应器的设计，但还包含催化剂床。生成的合成气温度与POX反应器的1,650K相比，为约1,300开尔文(K)。合成气温度的减少是重要的，因为催化剂不支持较高的温度值。ATR可以产生明显较高的合成气中H2与CO之比，并且还是无煤烟操作。
在典型的扩散燃烧器装置(未显示)中，燃料和氧化剂(少于约30体积百分比(vol％)的氧128和基本上纯的二氧化碳的稀释混合物)以非常激烈的方式混合以获得均匀的混合物并促进完全燃烧。本系统100使用基本纯的CO2以稀释氧化剂并提供温度控制。尽管低能量气体流112可能是足够纯的，在该类系统中作为稀释剂使用之前，仍然可能要求通过分子筛(mole sieve)、膜或其它方法(未显示)使之更纯化。外部燃烧器134可以被制成合适大小以提供燃烧完成所要求的停留时间，并获得EOR应用所要求的低氧水平。
图3是在有效的、低排放系统如图1A-1B所示的系统中生产烃的方法的示例性流程图。因此，可以参考图1A-1B最好地理解图3。方法300包括分离空气以形成高纯氧流和高纯氮流302，提供气态控制燃料流304，使所述控制燃料和高纯氧流燃烧以形成具有CO2和H2O的燃烧流306，接收燃烧流进入发电系统以至少产生压缩的、气态的、基本为二氧化碳的流308，将所述压缩的、气态的、基本为二氧化碳的流注入提高采收率法采油油藏310，以及将高纯氮流注入强化氮替代油藏312。
本发明的多个可选实施方式是可能的，其中一些在本文中被更详细地描述，其中的其它实施方式对本领域普通技术人员来说是显而易见的。在一个可选的实施方式中，水流155可经路线155′被送入HRSG144以产生更多蒸汽146。在另一可选的实施方式中，气态控制燃料流125至少部分地由烃流118′、烃流118的衍生流组成。这样的配置提供了另一集成协同作用并且可以降低系统100的总操作成本。进一步的可选实施方式包括从低能量流109截取滑流108′以向用于EOR的注入压缩机164提供CO2。这样的方法可以允许EOR在系统100的其它元件处于合适位置之前早处于方法中，或者可以根据系统100的要求简单地使各个流109和162平衡。
在另一可选的实施方式中，出于安全或控制原因，流108可以直接被送入燃烧器134或者气态控制燃料流125以与其预混合。在此预混合配置中，二氧化碳再循环流160可以基本上无烃以使流160可以被用作燃烧器134内的温度控制稀释剂。
在另一可选的实施方式中，所有的或部分的压缩二氧化碳流160被再循环至低能量流109。这一特别的实施方式在系统100的操作早期，例如在EOR行为需要之前，可能是有用的。在这种情况下，或许有利的是，提供额外量的CO2至燃烧器134用于温度控制和质量流量控制目的，以产生更多电力140用于出售或使用。特别地，如果有很少或没有EOR行为，压缩机164是不需要电力的，这节省了低排放产生的电力140用于出售或另外的目的。该可选动力装置循环也可以有利于产生大量的CO2用于出售或简单地使CO2聚集或分离直至EOR或其它目的需要。
下表提供可选再循环情况的气态流112、125、128、136、137和160(以及引入流112、125和128的摩尔流比率)的示例性组成，其中基本上是二氧化碳的流156经线路160被再循环至燃烧器134。
表2
Figure BPA00001231657000161
如从表中应该明显看出的，系统100的完全再循环实施方式形成了比以上表1中所述的完全注入情况稍微较高的CO2浓度，并且也包括较高的摩尔流量比率，这致使产生的CO2比注入情况中显著更多。
燃烧稳定性是本发明的一个重要方面。尽管有很多可能的方法提供化学计量的或接近化学计量条件的稳定燃烧，但这些许多方法被限制或技术上不可行。预热气态控制燃料流125以及低能量流112和112′并控制氧128和CO2混合物浓度是确保燃烧稳定性的所有可能的方法。系统100的一个可能的实施方式包括使部分气态排出流142或气态燃烧流136改变方向以加热流125、112和112′。
一些可选的燃烧选项包括向气态控制燃料流125或低能量气态流112添加氢，如美国专利号6,298,652所公开的。向气态控制燃料流125或低能量气态流112添加较重的烃(C2+)以确保燃烧稳定性或许还是经济的。可以独立购买这些较重的烃，或可以由线路118′提供。添加这些燃料可能需要额外的净化设备，所以这种方法的经济学应该被谨慎考虑。
在又一可选实施方式中，HRSG144中的热回收可以在升高的压力下进行。在这样的方法中，气态排出流142的体积可以显著减少，并且水在较高温度下凝结出来；这使得水的除去更易于完成，且使冷凝热在较高温度下可得到，这对于发电152或脱盐(未显示)更有价值。
图4图解图1A-1B的低排放发电系统的另一实施方式。因此，可以参考图1A-1B最好地理解图4。系统400包括生产第一混合流体烃采出流103的烃采收油藏102，并且包括分离机构104、液体烃产物流106、包含一些CO2和轻烃的第二气态原料流108——其可以与再循环流160混合以形成主要包含CO2的低能量流109、至少一个压缩机构110A-110X——其包括压缩机并可以包括冷却机构以压缩和冷却低能量气态原料流109来提供第一压缩低能量气态流112。系统400进一步包括外部燃烧器410以结合并燃烧高纯氧流128和控制燃料流125与压缩低能量气体流112，产生气态燃烧流136，气态燃烧流136可以与压缩的低能量侧流112′混合以形成膨胀器进入流137。热气体膨胀器420被提供，其接收膨胀器进入流137以产生能量140和膨胀的排出流142，排出流142可以被送至HRSG 144以经蒸汽轮机150产生蒸汽146和能量152。在蒸汽产生之后，流148可以被送至冷却机构154以冷凝并滴出水组分155，形成基本上为二氧化碳的流156，流156被送至CO2压缩机158，然后经线路160再循环或经线路162送至注入压缩机164用于注入EOR油藏167。要注意的是，流156的一部分可以被再循环而剩余部分被注入。
热气体膨胀器420可以是商业可得的机构，如来自General Electric的FEX-125或类似型号。但是，膨胀器420也可以是稍微改进的机构以在预期的温度和压力下处理基本为CO2的流体136。在一个示例性实施方式中，多个热气体膨胀器420A-420X将平行排列。尽管期望一些改进，但高压热气体膨胀器420是比集成的气体发电轮机更有效的设备。例如，在气体发电轮机中使用基本为CO2的工作流体136出现困难的且未解决的热力学和操作问题，它们可能需要重新设计基础(ground-up)轮机。参见例如美国专利申请号2007/0237696和SNARHEIM，DAGFINN等，Control Design for a Gas Turbine Cycle withCO2 Capture Capabilities，16th IFAC World Congress，Prague，Czech Rep.，July 2005。但是，热气体膨胀器没有气体发电轮机的复杂性。热气体膨胀器的使用增加了为提高性能而进行系统优化的自由度。例如，操作压力可被升高以增加Brayton动力循环的热力学效率。由于这些和其它原因，热气体膨胀器420与气体发电轮机相比可更适合于运行基本为CO2的工作流体排出气体136或137，而且可以不需要新设计。
图5是操作图4中系统的示例性方法。因此，可以参考图1A-1B和4最好地理解图5。方法500包括产生和分离502烃流102以形成压缩的低能量气体流112，提供504高纯氧流128，提供506气态控制燃料流125，在外部燃烧器410中燃烧508至少高纯氧流128和气态控制燃料流125的组合以产生含二氧化碳和水的气态燃烧流136，在热气体膨胀器420中使气态燃烧流136或137膨胀510，以产生至少一个单位的机械能140和气态排出流142，从气态排出流148中除去512至少一部分水组分155，以及使用514生成的二氧化碳组分156的至少一部分。
图6图解图4的低排放发电系统的另一实施方式。因此，可以参考图1A-1B和4最好地理解图6。系统600包括与系统100、101和400相同的许多组件。但是，系统600使用气体发电轮机620代替热气体膨胀器420。轮机入口压缩机605被配置为接收大气121，通过管道或类似机构605连接至膨胀器620，且包括燃烧器610。
在这样的系统600中，气体发电轮机将仍使用压缩的低能量气体流112作为工作流体以冷却系统，因为来自入口压缩机605的压缩空气123被用在空气分离机构124中。在一个特别的实施方式中，压缩空气流123的体积流量将产生足够满足燃烧器134内化学计量反应所需要的氧量的高纯氧流128。
图7是操作图6系统的示例性方法。因此，可以参考图1A-1B和6最好地理解图7。方法700包括产生和分离702烃流102以形成压缩的低能量气体流112，在配置为产生至少高纯氧流128的空气分离机构124中分离空气704，提供706气态控制燃料流125，在燃烧器610内燃烧708、至少高纯氧流128和气态控制燃料流125的组合以产生含二氧化碳和水的气态燃烧流136，在燃气轮机的膨胀器620中使气态燃烧流136或137膨胀710以产生至少一个单位的机械能140和气态排出流142，在气体发电轮机605的入口压缩机中压缩空气712以形成压缩空气流123，将压缩空气流123提供714到空气分离机构124，从气态排出流148中除去716至少一部分水组分155，以及使用718生成的二氧化碳组分156的至少一部分。
图8A-8C图解图1A-1B的低排放发电系统的另外的可选实施方式。因此，可以参考图1A-1B最好地理解图8A-8C。图8A图解用于生产烃的系统800，其中来自压缩机110a-110x的压缩低能量气体流802可以在燃烧器134内混合和燃烧前通过HRSG 144，以热调节(例如冷却)低能量气体流802。系统800进一步包括处于压缩机110a-110x和膨胀器138之间的管道804，以形成动力轮机(power turbine)。另外，冷却机构154产生基本为二氧化碳的流806，其可以被至少部分再循环到压缩机110a-110x和/或转移到流808至压缩机164用于注入和/或分离、储存或排出。一旦再循环回路通过线路806建立起来，可能不需要线路108，除非用于补充低热值燃料的量。在又一可选实施方式中，线路108可以被直接转移到燃烧器134作为稀释剂或被转移到线路125与气态流108和125在燃烧前预混。图8B图解了系统820，其与系统800非常相似，除了基本为二氧化碳的流808B从流802中被转移。图8C图解系统840，其与系统820非常相似，除了其不通过管道(shaft)804合并压缩机110a-110x与膨胀器138。
在系统100、101、400、600、800、820或840的任何一个中，优选避免昂贵的和能量密集的CO2分离设备。为了实现该目标，氧流128的纯度可以足以限制杂质的存在，从而避免另外的分离设备或方法。
在一些实施方式中，系统100、101、400、600、800、820或840的至少一部分可被设置在海上驳轮或平台上。在这样的系统中，能量可在海上或陆上被利用，且油藏113、171、102和167的至少一个也可以位于海上位置。
在公开的系统和方法的一些实施方式中，燃料杂质也可以被考虑。应当只考虑产生可满足EOR规格的副产物的燃料，或处于足够高的经济优势以使去除它们的加工装备可被认为是适当的燃料。
在氩气市场存在的情况下，ASU 124中用于其分离的额外成本、能量和复杂性可以认为是适当的。
虽然本发明可能有各种改进和可选形式，但以上讨论的示例性实施方式仅以实例的方式被显示。然而，还应该理解本发明并不意欲限于本文公开的特定实施方式。事实上，本发明包括落入所附权利要求的真正精神和范围内的所有替代方式、改进和等同物。

Claims (59)

1.集成系统，包括：
空气分离机构，其被配置为产生高纯氧流和高纯氮流；
气态控制燃料流；
燃烧机构，其被配置为使至少所述气态控制燃料流和所述高纯氧流在接近化学计量但稍微燃料富余的条件下燃烧，以产生含二氧化碳和水的气态燃烧流；
至少包括膨胀器的发电系统，其被配置为接收所述含二氧化碳和水的气态燃烧流并至少产生压缩的、气态的、基本为二氧化碳的流；
第一注入器机构，其被配置为将所述压缩的、气态的、基本为二氧化碳的流的至少一部分注入提高采收率法采油油藏；和
第二注入器机构，其被配置为将所述高纯氮流的至少一部分注入压力保持油藏。
2.根据权利要求1所述的系统，其中所述膨胀器被配置为接收所述气态燃烧流并产生至少一个单位的机械能和气态排出流；并且所述发电系统进一步包括：
热回收机构，其被配置为接收并冷却所述气态排出流，产生至少一个单位的热能，并生成至少一体积的水和冷却的、气态的、基本上为二氧化碳的流，其中所述热能任选地被利用以生成产生蒸汽能的蒸汽；和
二氧化碳压缩机，其被配置为压缩所述冷却的、气态的、基本上为二氧化碳的流以产生所述压缩的、气态的、基本为二氧化碳的流。
3.权利要求2所述的系统，进一步包括：
第一烃采收油藏，其被配置为产生第一烃混合物；和
第一烃分离机构，其被配置为至少将液体烃从所述第一烃混合物中分离出来并产生第一烃流和包括二氧化碳和烃的第二气体流，其中所述燃烧机构被进一步配置为利用所述第二气体流的至少一部分与所述气态控制燃料流和所述高纯氧流，产生所述含二氧化碳和水的气态燃烧流。
4.权利要求3所述的系统，进一步包括：
第二烃采收油藏，其被配置为产生第二烃混合物；和
第二烃分离机构，其被配置为至少将液体烃从所述第二烃混合物中分离出来并产生第二烃流和包括氮气的惰性气体流，其中所述第二注入器进一步被配置以将所述惰性气体流注入所述压力保持油藏。
5.根据权利要求4所述的系统，其中所述提高采收率法采油油藏选自：所述第一烃采收油藏、所述第二烃采收油藏、另一烃采收油藏及其任意组合。
6.根据权利要求4所述的系统，其中所述压力保持油藏选自：所述第一烃采收油藏、所述第二烃采收油藏、另一烃采收油藏及其任意组合。
7.权利要求3所述的系统，进一步包括再循环回路，其被配置为将所述压缩的、气态的、基本为二氧化碳的流的至少一部分引向所述燃烧机构或所述第二气体流。
8.权利要求3所述的系统，进一步包括控制算法，其被配置为控制所述气态控制燃料流、所述包含二氧化碳和烃的第二气体流和所述高纯氧流的混合和燃烧，以确保所述高纯氧流内基本上所有氧耗尽。
9.根据权利要求8所述的系统，其中所述燃烧机构选自：氧燃烧器、预混合燃烧器、点火燃烧器、部分氧化(POX)燃烧器、扩散燃烧器、自热重整器和oxyClaus反应炉燃烧器。
10.根据权利要求2所述的系统，其中所述膨胀器选自：气体发电轮机中的膨胀器和热气体膨胀器。
11.权利要求10所述的系统，进一步包括入口压缩机，其被配置为压缩大气以形成压缩空气流，其中所述空气分离机构被配置以利用所述压缩空气流形成所述高纯氧流和所述高纯氮流。
12.根据权利要求11所述的系统，其中所述膨胀器是所述气体发电轮机中的膨胀器，并且所述入口压缩机被所述气体发电轮机驱动，以及所述压缩的、气态的、基本为二氧化碳的流被用作所述气体发电轮机的膨胀器内的工作流体。
13.根据权利要求4所述的系统，其中所述包括二氧化碳和烃的第二气体流包含60体积百分比的二氧化碳至95体积百分比的二氧化碳；
其中所述高纯氧流包含70体积百分比的氧至100体积百分比的氧；
其中所述含氮的惰性气体流包含70体积百分比的氮至100体积百分比的氮；
其中所述气态控制燃料流包含80体积百分比至100体积百分比的甲烷；以及
其中所述高纯氮流包含85体积百分比的氮至100体积百分比的氮。
14.根据权利要求1-2的任何一项所述的系统，其中所述高纯氮流的至少一部分被送至选自以下的场所：氮储存场所、氮出售场所和氮排出场所。
15.权利要求3所述的系统，进一步包括第二气体压缩机，其被配置为压缩所述包括二氧化碳和烃的第二气体流以形成压缩的第二气体流，之后将所述压缩的第二气体流的至少一部分送至所述燃烧机构。
16.根据权利要求1-2的任何一项所述的系统，其中所述压缩的、气态的、基本为二氧化碳的流的至少一部分被送至选自以下的场所：二氧化碳分离场所、二氧化碳出售场所、碳捕集场所、排出场所及其任意组合。
17.权利要求11所述的系统，进一步包括脱盐设备，其被配置为利用所述机械能、所述蒸汽能、所述至少一个单位的热能和所述入口压缩机产生的热的至少一种。
18.权利要求15所述的系统，进一步包括交叉交换加热系统，其被配置为将从热源产生的热的至少一部分转移至所述压缩的第二气体流，其中所述热源选自：所述二氧化碳压缩机、所述热回收机构、所述气态燃烧流、所述气态排出流及其任意组合。
19.根据权利要求2所述的系统，其中所述气态排出流在大气压以上被提供至所述热回收机构。
20.改进的烃采收方法，包括：
将空气分离成高纯氧流和高纯氮流；
提供气态控制燃料流；
在燃烧器内使至少所述气态控制燃料流和所述高纯氧流在接近化学计量但稍微燃料富余的条件下燃烧以形成含二氧化碳和水的气态燃烧流；
将所述含二氧化碳和水的气态燃烧流接收入至少包括膨胀器的发电系统，其中所述发电系统至少产生压缩的、气态的、基本上为二氧化碳的流；
将所述压缩的、气态的、基本上为二氧化碳的流的至少一部分注入提高采收率法采油油藏；和
将所述高纯氮流的至少一部分注入压力保持油藏。
21.根据权利要求20所述的方法，其中所述膨胀器使所述气态燃烧流膨胀以产生至少一个单位的机械能和气态排出流；操作所述发电系统的方法进一步包括：
在配置的热回收机构内冷却所述气态排出流，以产生至少一个单位的热能，冷却的、气态的、基本上为二氧化碳的流和一体积的水，其中所述至少一个单位的热能任选地被利用以产生用于产生至少一个单位的蒸汽能的蒸汽；和
在二氧化碳压缩机内压缩所述冷却的、气态的、基本上为二氧化碳的流以形成所述压缩的、气态的、基本为二氧化碳的流。
22.权利要求21所述的方法，进一步包括：
从第一烃采收油藏产生第一烃混合物；
将所述第一烃混合物分离为第一烃流和包括二氧化碳和烃的第二气体流；和
将所述包括二氧化碳和烃的第二气体流的至少一部分送至：1)所述气态控制燃料流以混合，或者2)燃烧所述气态控制燃料流和所述高纯氧流的步骤中的所述燃烧器。
23.权利要求22所述的方法，进一步包括：
从第二烃采收油藏产生第二烃混合物；
将所述第二烃混合物分离为第二烃流和含氮的惰性气体流；和
将所述含氮的惰性气体流加入所述高纯氮流用于注入所述压力保持油藏。
24.权利要求22所述的方法，进一步包括在将所述第二气体流的至少一部分送至所述燃烧器之前压缩所述包括二氧化碳和烃的第二气体流以形成压缩的第二气体流。
25.权利要求22所述的方法，进一步包括使所述压缩的、气态的、基本为二氧化碳的流的至少一部分再循环至所述燃烧器或所述第二气体流。
26.权利要求21所述的方法，进一步包括提供所述一体积的水的至少一部分用作灌溉水或用于产生蒸汽。
27.根据权利要求21所述的方法，其中所述膨胀器选自：气体发电轮机内的膨胀器和热气体膨胀器。
28.权利要求27所述的方法，进一步包括在入口压缩机内压缩大气；和
在空气分离机构内利用压缩空气以形成所述高纯氧流和所述高纯氮流。
29.根据权利要求28所述的方法，其中所述膨胀器是所述气体发电轮机内的膨胀器，所述入口压缩机被所述气体发电轮机驱动；和
利用所述压缩的、气态的、基本为二氧化碳的流作为所述气体发电轮机内的工作流体。
30.根据权利要求23所述的方法，其中所述包括二氧化碳和烃的第二气体流包括60体积百分比的二氧化碳至95体积百分比的二氧化碳；
其中所述高纯氧流包含70体积百分比的氧至100体积百分比的氧；
其中所述含氮的惰性气体流包含70体积百分比的氮至100体积百分比的氮；
其中所述气态控制燃料流包含80体积百分比至100体积百分比的甲烷；以及
其中所述高纯氮流包含85体积百分比的氮至100体积百分比的氮。
31.根据权利要求23所述的方法，其中所述提高采收率法采油油藏选自：所述第一烃采收油藏、所述第二烃采收油藏、另一烃采收油藏及其任意组合。
32.根据权利要求23所述的方法，其中所述压力保持油藏选自：所述第二烃采收油藏、所述第一烃采收油藏、另一烃采收油藏及其任意组合。
33.权利要求24所述的方法，进一步包括利用选自以下的热源加热所述压缩的第二气体流的至少一部分：通过压缩所述冷却的、气态的、基本上为二氧化碳的流产生的热；通过压缩大气产生的热；来自所述含二氧化碳和水的气态燃烧流的热；来自所述气态排出流的热；所述至少一个单位的热能及其任意组合。
34.权利要求28所述的方法，进一步包括利用选自以下的热源加热所述压缩的第二气体流的至少一部分：通过压缩所述冷却的、气态的、基本上为二氧化碳的流产生的热；通过压缩大气产生的热；来自所述含二氧化碳和水的气态燃烧流的热；来自所述气态排出流的热；所述至少一个单位的热能及其任意组合。
35.权利要求22所述的方法，进一步包括控制所述气态控制燃料流、所述包括二氧化碳和烃的第二气体流以及所述高纯氧流的混合和燃烧，以确保高纯氧流内基本上所有氧耗尽。
36.根据权利要求35所述的方法，其中所述燃烧器选自：氧燃烧器、预混合燃烧器、点火燃烧器、部分氧化(POX)燃烧器、扩散燃烧器、自热重整器和oxyClaus反应炉燃烧器。
37.权利要求21所述的方法，进一步包括在脱盐设备中使水脱盐，其中所述脱盐设备利用所述至少一个单位的机械能、所述至少一个单位的热能、所述至少一个单位的蒸汽能、通过压缩所述冷却的、气态的、基本上为二氧化碳的流产生的热、来自所述含二氧化碳和水的气态燃烧流的热、来自所述气态排出流的热中的至少一个，及其任意组合。
38.根据权利要求21所述的方法，其中所述气态排出流在大气压以上被提供至所述热回收机构。
39.权利要求20所述的方法，进一步包括将所述压缩的、气态的、基本为二氧化碳的流的至少一部分送至选自以下的场所：二氧化碳分离场所、二氧化碳出售场所、碳捕集场所及其任意组合；以及
将所述高纯氮流的至少一部分送至氮储存场所。
40.低排放发电系统，包括：
第一烃采收油藏，其被配置为产生第一烃混合物；
第一烃分离机构，其被配置为至少将液体烃从所述第一烃混合物中分离出来并产生第一烃流和包括二氧化碳的第二气体流；
气态控制燃料流；
高纯氧流；
外部燃烧器，其被配置为使所述气态控制燃料流、所述高纯氧流和所述包含二氧化碳的第二气体流的组合在接近化学计量但稍微燃料富余的条件下燃烧以产生气态燃烧流；
热气体膨胀器，其被配置为接收所述气态燃烧流并产生至少一个单位的机械能和至少具有二氧化碳组分和水组分的气态排出流；和
操作系统，其被配置为调节所述气态排出流以充分地从中除去所述水组分并利用所述二氧化碳组分的至少一部分。
41.根据权利要求40所述的系统，其中所述操作系统进一步包括：
热回收机构，其被配置为接收所述气态排出流并产生一体积的水，冷却的、气态的、基本上为二氧化碳的流，和热能，其中所述热能任选地被利用以产生蒸汽，其中所述蒸汽的至少一部分被利用以产生蒸汽能；和
压缩机，其被配置为压缩所述冷却的、气态的、基本上为二氧化碳的流以产生压缩的、气态的、基本为二氧化碳的流。
42.根据权利要求41所述的系统，所述操作系统进一步包括：
再循环回路，其被配置为将所述压缩的、气态的、基本为二氧化碳的流的至少一部分引向所述外部燃烧器和所述包含二氧化碳的第二气体流的至少一个。
43.根据权利要求41所述的系统，其中所述压缩的、气态的、基本为二氧化碳的流的至少一部分被用在选自以下的系统中：用于将所述压缩的、气态的、基本为二氧化碳的流的至少一部分注入提高采收率法采油油藏和二氧化碳分离场所之一的系统，用于将所述压缩的、气态的、基本为二氧化碳的流的至少一部分改向至二氧化碳捕集场所、排出场所、二氧化碳出售场所中的一个及其任意组合的系统。
44.根据权利要求41所述的系统，其中所述外部燃烧器选自：氧燃烧器、预混合燃烧器、点火燃烧器、部分氧化(POX)燃烧器、扩散燃烧器、自热重整器和oxyClaus反应炉燃烧器。
45.低排放发电的方法，包括：
从第一烃采收油藏产生第一烃混合物；
将所述第一烃混合物分离为第一烃流和包括二氧化碳的第二气体流；
提供高纯氧流；
提供气态控制燃料流；
在外部燃烧器内使至少所述高纯氧流和所述气态控制燃料流的组合在接近化学计量但稍微燃料富余的条件下燃烧以产生含二氧化碳和水的气态燃烧流；
使所述气态燃烧流在热气体膨胀器内膨胀以产生至少一个单位的机械能及至少具有水组分和二氧化碳组分的气态排出流；
从所述气态排出流中除去所述水组分的至少一部分；和
利用所述气态排气流的所述二氧化碳组分的至少一部分。
46.权利要求45所述的方法，进一步包括：
在热回收机构内冷却所述气态排出流，其中所述冷却产生一体积的水，冷却的、气态的、基本上为二氧化碳的流，和热能，其中所述热能任选地被利用以产生蒸汽，其中所述蒸汽的至少一部分被用于产生蒸汽能；和
压缩所述冷却的、气态的、基本上为二氧化碳的流以产生压缩的、气态的、基本为二氧化碳的流。
47.权利要求46所述的方法，进一步包括将压缩的、气态的、基本为二氧化碳的流的至少一部分再循环至所述外部燃烧器和所述包括二氧化碳的第二气体流中的至少一个。
48.根据权利要求46所述的方法，其中所述压缩的、气态的、基本为二氧化碳的流的至少一部分被用在选自以下的方法中：将压缩的、气态的、基本为二氧化碳的流的至少一部分注入提高采收率法采油油藏和二氧化碳分离场所中的至少一个，将压缩的、气态的、基本为二氧化碳的流的至少一部分改向至碳捕集场所和二氧化碳出售场所中的一个，及其任意组合。
49.低排放发电系统，包括：
第一烃采收油藏，其被配置为产生第一烃混合物；
第一烃分离机构，其被配置为至少将液体烃从所述第一烃混合物中分离出来并产生第一烃流和包括二氧化碳的第二气体流；
气态控制燃料流；
空气分离机构，其被配置为至少提供高纯氧流；
燃烧器，其被配置为使所述气态控制燃料流、所述高纯氧流和所述包括二氧化碳的第二气体流的组合在接近化学计量但稍微燃料富余的条件下燃烧以产生气态燃烧流；
气体发电轮机，所述气体发电轮机包括：
入口压缩机，其中所述入口压缩机被配置为压缩大气以送至所述空气分离机构；和
膨胀器，其被配置为接收所述气态燃烧流并产生至少一个单位的机械能和至少具有二氧化碳组分和水组分的气态排出流；和
操作系统，其被配置为调节所述气态排出流以充分地除去所述气态排出流的水组分并利用所述气态排出流的所述二氧化碳组分的至少一部分。
50.根据权利要求49所述的系统，所述操作系统进一步包括：
热回收机构，其被配置为接收所述气态排出流并产生热，一体积的水和冷却的、气态的、基本上为二氧化碳的流，其中所述热任选地被利用以产生用于产生蒸汽能的蒸汽；和
压缩机，其被配置为压缩所述冷却的、气态的、基本上为二氧化碳的流以产生压缩的、气态的、基本为二氧化碳的流。
51.根据权利要求50所述的系统，所述操作系统进一步包括：
再循环回路，其被配置为将所述压缩的、气态的、基本为二氧化碳的流的至少一部分引向所述燃烧器和所述包括二氧化碳的第二气体流中的一个。
52.根据权利要求50所述的系统，其中所述压缩的、气态的、基本为二氧化碳的流的至少一部分被用在选自以下的方法中：将压缩的、气态的、基本为二氧化碳的流的至少一部分注入提高采收率法采油油藏和二氧化碳分离场所中的至少一个，将压缩的、气态的、基本为二氧化碳的流的至少一部分改向至碳捕集场所和二氧化碳出售场所中的一个，及其任意组合。
53.根据权利要求50所述的系统，其中所述水组分被用于产生所述蒸汽和灌溉中的一种。
54.低排放发电方法，包括：
从第一烃采收油藏产生第一烃混合物；
将所述第一烃混合物分离为第一烃流和包括二氧化碳的第二气体流；
在空气分离机构内分离空气，所述空气分离机构被配置以至少产生高纯氧流；
提供气态控制燃料流；
在燃烧器内使至少所述高纯氧流和所述气态控制燃料流的组合在接近化学计量但稍微燃料富余的条件下燃烧以产生含二氧化碳和水的气态燃烧流；
在气体发电轮机的入口压缩机内压缩空气以形成压缩的空气流；
将所述压缩的空气流提供至所述空气分离机构；
使所述气态燃烧流在所述气体发电轮机的膨胀器内膨胀以产生至少一个单位的机械能和至少具有水组分和二氧化碳组分的气态排出流；
从所述气态排出流中除去所述水组分的至少一部分；和利用所述二氧化碳组分的至少一部分。
55.权利要求54所述的方法，进一步包括：
在热回收机构内冷却所述气态排出流，其中所述冷却产生一体积的水，冷却的、气态的、基本上为二氧化碳的流和热，其中所述热任选地被利用以产生蒸汽，所述蒸汽用于产生至少一个单位的蒸汽能；和
压缩所述冷却的、气态的、基本上为二氧化碳的流以产生压缩的、气态的、基本为二氧化碳的流。
56.权利要求55所述的方法，进一步包括将所述压缩的、气态的、基本为二氧化碳的流的至少一部分再循环至所述燃烧器和所述包括二氧化碳的第二气体流中的一个。
57.根据权利要求55所述的方法，其中所述压缩的、气态的、基本为二氧化碳的流的至少一部分被用在选自以下的方法中：将压缩的、气态的、基本为二氧化碳的流的至少一部分注入提高采收率法采油油藏和二氧化碳分离场所中的至少一个，将压缩的、气态的、基本为二氧化碳的流的至少一部分改向至碳捕集场所和二氧化碳出售场所中的一个，及其任意组合。
58.根据权利要求56所述的方法，其中所述水组分被用于产生所述蒸汽和灌溉中的一种。
59.根据权利要求1、40和49中任何一项所述的系统，其中所述系统的至少一部分位于海上驳船或平台上。
CN200980111019.0A 2008-03-28 2009-03-25 低排放发电和烃采收系统及方法 Expired - Fee Related CN101981272B (zh)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
US7229208P 2008-03-28 2008-03-28
US61/072,292 2008-03-28
US15350809P 2009-02-18 2009-02-18
US61/153,508 2009-02-18
PCT/US2009/038247 WO2009120779A2 (en) 2008-03-28 2009-03-25 Low emission power generation and hydrocarbon recovery systems and methods

Publications (2)

Publication Number Publication Date
CN101981272A CN101981272A (zh) 2011-02-23
CN101981272B true CN101981272B (zh) 2014-06-11

Family

ID=41114672

Family Applications (1)

Application Number Title Priority Date Filing Date
CN200980111019.0A Expired - Fee Related CN101981272B (zh) 2008-03-28 2009-03-25 低排放发电和烃采收系统及方法

Country Status (7)

Country Link
US (1) US8984857B2 (zh)
EP (1) EP2268897B1 (zh)
CN (1) CN101981272B (zh)
AU (1) AU2009228283B2 (zh)
CA (3) CA2715186C (zh)
MY (1) MY156350A (zh)
WO (1) WO2009120779A2 (zh)

Families Citing this family (104)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7644993B2 (en) * 2006-04-21 2010-01-12 Exxonmobil Upstream Research Company In situ co-development of oil shale with mineral recovery
CN101595273B (zh) * 2006-10-13 2013-01-02 埃克森美孚上游研究公司 用于原位页岩油开发的优化的井布置
US8622133B2 (en) * 2007-03-22 2014-01-07 Exxonmobil Upstream Research Company Resistive heater for in situ formation heating
US20080290719A1 (en) 2007-05-25 2008-11-27 Kaminsky Robert D Process for producing Hydrocarbon fluids combining in situ heating, a power plant and a gas plant
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
SG195533A1 (en) 2008-10-14 2013-12-30 Exxonmobil Upstream Res Co Methods and systems for controlling the products of combustion
EP2364198A2 (en) 2008-12-04 2011-09-14 E. I. du Pont de Nemours and Company Carbon dioxide removal and ionic liquid compounds useful therein
CA2750405C (en) * 2009-02-23 2015-05-26 Exxonmobil Upstream Research Company Water treatment following shale oil production by in situ heating
SG176670A1 (en) 2009-06-05 2012-01-30 Exxonmobil Upstream Res Co Combustor systems and methods for using same
EA023673B1 (ru) * 2009-11-12 2016-06-30 Эксонмобил Апстрим Рисерч Компани Система и способ для низкоэмиссионного производства электроэнергии и извлечения углеводородов
US8863839B2 (en) * 2009-12-17 2014-10-21 Exxonmobil Upstream Research Company Enhanced convection for in situ pyrolysis of organic-rich rock formations
US9067953B2 (en) * 2010-03-12 2015-06-30 E I Du Pont De Nemours And Company Systems for carbon dioxide and sulfur dioxide removal
US9017455B2 (en) 2010-06-03 2015-04-28 E I Du Pont De Nemours And Company Sulfur compounds for carbon dioxide and sulfur dioxide removal
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
MY156099A (en) 2010-07-02 2016-01-15 Exxonmobil Upstream Res Co Systems and methods for controlling combustion of a fuel
PL2588727T3 (pl) 2010-07-02 2019-05-31 Exxonmobil Upstream Res Co Spalanie stechiometryczne z recyrkulacją gazów spalinowych i chłodnicą bezpośredniego kontaktu
BR112012031153A2 (pt) 2010-07-02 2016-11-08 Exxonmobil Upstream Res Co sistemas e métodos de geração de energia de triplo-ciclo de baixa emissão
JP5913305B2 (ja) 2010-07-02 2016-04-27 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 低エミッション発電システム及び方法
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
EP2601393B1 (en) 2010-08-06 2020-01-15 Exxonmobil Upstream Research Company Systems and methods for optimizing stoichiometric combustion
WO2012018458A1 (en) 2010-08-06 2012-02-09 Exxonmobil Upstream Research Company System and method for exhaust gas extraction
US8616280B2 (en) 2010-08-30 2013-12-31 Exxonmobil Upstream Research Company Wellbore mechanical integrity for in situ pyrolysis
WO2012030426A1 (en) 2010-08-30 2012-03-08 Exxonmobil Upstream Research Company Olefin reduction for in situ pyrolysis oil generation
US20120118004A1 (en) * 2010-11-12 2012-05-17 Exxonmobil Research And Engineering Company Adsorption chilling for compressing and transporting gases
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
TWI563165B (en) 2011-03-22 2016-12-21 Exxonmobil Upstream Res Co Power generation system and method for generating power
TWI563166B (en) 2011-03-22 2016-12-21 Exxonmobil Upstream Res Co Integrated generation systems and methods for generating power
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
US8671659B2 (en) * 2011-04-29 2014-03-18 General Electric Company Systems and methods for power generation using oxy-fuel combustion
CA2836814C (en) * 2011-05-24 2016-09-27 Her Majesty The Queen In Right Of Canada As Represented By The Ministeof Natural Resources High pressure fossil fuel oxy-combustion system with carbon dioxide capture for interface with an energy conversion system
WO2013062754A1 (en) * 2011-10-26 2013-05-02 Exxonmobil Upstream Research Company Low emission heating of a hydrocarbon formation
CA2845012A1 (en) 2011-11-04 2013-05-10 Exxonmobil Upstream Research Company Multiple electrical connections to optimize heating for in situ pyrolysis
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
NO20111770A1 (no) 2011-12-21 2011-12-21 Modi Vivendi As System og metode for offshore industrielle aktiviteter med CO2 reinjisering
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
AU2013256823B2 (en) 2012-05-04 2015-09-03 Exxonmobil Upstream Research Company Systems and methods of detecting an intersection between a wellbore and a subterranean structure that includes a marker material
TWI630021B (zh) 2012-06-14 2018-07-21 艾克頌美孚研究工程公司 用於ｃｏ捕捉／利用和ｎ製造之變壓吸附與發電廠的整合
WO2014028832A1 (en) * 2012-08-16 2014-02-20 University Of South Florida Systems and methods for water desalination and power generation
AU2013332312B2 (en) * 2012-10-16 2016-05-05 Exxonmobil Upstream Research Company Increasing combustibility of low BTU natural gas
US9631815B2 (en) 2012-12-28 2017-04-25 General Electric Company System and method for a turbine combustor
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
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
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
US9708977B2 (en) 2012-12-28 2017-07-18 General Electric Company System and method for reheat in gas turbine with exhaust gas recirculation
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
US9574496B2 (en) 2012-12-28 2017-02-21 General Electric Company System and method for a 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
US9869279B2 (en) 2012-11-02 2018-01-16 General Electric Company System and method for a multi-wall turbine combustor
US9803865B2 (en) 2012-12-28 2017-10-31 General Electric Company System and method for a turbine combustor
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
US9938861B2 (en) 2013-02-21 2018-04-10 Exxonmobil Upstream Research Company Fuel combusting method
TW201502356A (zh) 2013-02-21 2015-01-16 Exxonmobil Upstream Res Co 氣渦輪機排氣中氧之減少
RU2637609C2 (ru) 2013-02-28 2017-12-05 Эксонмобил Апстрим Рисерч Компани Система и способ для камеры сгорания турбины
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
US9784182B2 (en) 2013-03-08 2017-10-10 Exxonmobil Upstream Research Company Power generation and methane recovery from methane hydrates
US20140250945A1 (en) 2013-03-08 2014-09-11 Richard A. Huntington Carbon Dioxide Recovery
US9618261B2 (en) 2013-03-08 2017-04-11 Exxonmobil Upstream Research Company Power generation and LNG production
EP2784288B1 (de) * 2013-03-28 2020-02-19 Lumenion AG Kraftwerksanlage und Verfahren zum Erzeugen von elektrischem Strom
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
US9617914B2 (en) 2013-06-28 2017-04-11 General Electric Company Systems and methods for monitoring gas turbine systems having exhaust gas recirculation
US9835089B2 (en) 2013-06-28 2017-12-05 General Electric Company System and method for a fuel nozzle
US9631542B2 (en) 2013-06-28 2017-04-25 General Electric Company System and method for exhausting combustion gases from gas turbine engines
JP6220586B2 (ja) * 2013-07-22 2017-10-25 ８ リバーズ キャピタル，エルエルシー ガスタービン設備
US9587510B2 (en) 2013-07-30 2017-03-07 General Electric Company System and method for a gas turbine engine sensor
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
US9951658B2 (en) 2013-07-31 2018-04-24 General Electric Company System and method for an oxidant heating system
CN104234864B (zh) * 2013-09-12 2016-03-16 摩尔动力(北京)技术股份有限公司 气闭合发动机
AU2014340644B2 (en) 2013-10-22 2017-02-02 Exxonmobil Upstream Research Company Systems and methods for regulating an in situ pyrolysis process
US9394772B2 (en) 2013-11-07 2016-07-19 Exxonmobil Upstream Research Company Systems and methods for in situ resistive heating of organic matter in a subterranean formation
US10030588B2 (en) 2013-12-04 2018-07-24 General Electric Company Gas turbine combustor diagnostic system and method
US9752458B2 (en) 2013-12-04 2017-09-05 General Electric Company System and method for a gas turbine engine
US10227920B2 (en) 2014-01-15 2019-03-12 General Electric Company Gas turbine oxidant separation system
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
US9863267B2 (en) 2014-01-21 2018-01-09 General Electric Company System and method of control for a gas turbine engine
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
US9885290B2 (en) 2014-06-30 2018-02-06 General Electric Company Erosion suppression system and method in an exhaust gas recirculation gas turbine system
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
US10060348B2 (en) * 2014-09-25 2018-08-28 Air Products And Chemicals, Inc. Membrane separation of carbon dioxide from natural gas with energy recovery
US9644466B2 (en) 2014-11-21 2017-05-09 Exxonmobil Upstream Research Company Method of recovering hydrocarbons within a subsurface formation using electric current
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
US9869247B2 (en) 2014-12-31 2018-01-16 General Electric Company Systems and methods of estimating a combustion equivalence ratio in a gas turbine with exhaust gas recirculation
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
US10316746B2 (en) 2015-02-04 2019-06-11 General Electric Company Turbine system with exhaust gas recirculation, separation and extraction
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
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
WO2017087154A1 (en) 2015-11-17 2017-05-26 Exxonmobil Research And Engineering Company Staged pressure swing adsorption for simultaneous power plant emission control and enhanced hydrocarbon recovery
WO2017087167A1 (en) 2015-11-17 2017-05-26 Exxonmobil Research And Engineering Company Staged complementary psa system for low energy fractionation of mixed fluid
US10071337B2 (en) 2015-11-17 2018-09-11 Exxonmobil Research And Engineering Company Integration of staged complementary PSA system with a power plant for CO2 capture/utilization and N2 production
WO2017087153A1 (en) 2015-11-17 2017-05-26 Exxonmobil Research And Engineering Company Fuel combusting method with co2 capture
WO2017087165A1 (en) 2015-11-17 2017-05-26 Exxonmobil Research And Engineering Company Hybrid high-temperature swing adsorption and fuel cell
US10125641B2 (en) 2015-11-17 2018-11-13 Exxonmobil Research And Engineering Company Dual integrated PSA for simultaneous power plant emission control and enhanced hydrocarbon recovery
FR3055923B1 (fr) 2016-09-09 2022-05-20 Eric Bernard Dupont Systeme mecanique de production d'energie mecanique a partir d'azote liquide et procede correspondant
WO2019113575A1 (en) * 2017-12-08 2019-06-13 Schlumberger Technology Corporation Compressed n2 for energy storage
US20220316304A1 (en) * 2021-04-02 2022-10-06 Exmar Offshore Company Offshore oil and gas power generation with carbon capture and beneficial use of co2

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4434613A (en) * 1981-09-02 1984-03-06 General Electric Company Closed cycle gas turbine for gaseous production
CN1451844A (zh) * 2003-05-09 2003-10-29 辽河石油勘探局 一种油田开采热、电、co2、n2联供制造方法

Family Cites Families (665)

* Cited by examiner, † Cited by third party
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
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
US3147805A (en) * 1962-01-19 1964-09-08 Gulf Research Development Co Method for consolidating an unconsolidated formation
US3292701A (en) * 1963-11-12 1966-12-20 Gulf Research Development Co Method for consolidating incompetent subsurface formations
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
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.
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
US4637792A (en) 1980-12-22 1987-01-20 Arkansas Patents, Inc. Pulsing combustion
US4480985A (en) 1980-12-22 1984-11-06 Arkansas Patents, Inc. Pulsing combustion
US4479484A (en) 1980-12-22 1984-10-30 Arkansas Patents, Inc. Pulsing combustion
US4488865A (en) 1980-12-22 1984-12-18 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
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
US4548267A (en) * 1983-11-29 1985-10-22 Standard Oil Company Method of displacing fluids within a gas-condensate reservoir
US4635721A (en) * 1983-11-29 1987-01-13 Amoco Corporation Method of displacing fluids within a gas-condensate reservoir
US4602614A (en) 1983-11-30 1986-07-29 United Stirling, Inc. Hybrid solar/combustion powered receiver
US4690219A (en) * 1984-03-05 1987-09-01 Phillips Petroleum Company Acidizing using n-vinyl lactum/unsaturated amide copolymers
US4578201A (en) * 1984-03-05 1986-03-25 Phillips Petroleum Company N-vinyl lactam/unsaturated amide copolymers in thickened acid compositions
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
US5050375A (en) * 1985-12-26 1991-09-24 Dipac Associates Pressurized wet combustion at increased temperature
US4714032A (en) * 1985-12-26 1987-12-22 Dipac Associates Pollution-free pressurized combustion utilizing a controlled concentration of water vapor
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
US4765407A (en) * 1986-08-28 1988-08-23 Amoco Corporation Method of producing gas condensate and other reservoirs
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
US4899544A (en) * 1987-08-13 1990-02-13 Boyd Randall T Cogeneration/CO2 production process and plant
US4747858A (en) * 1987-09-18 1988-05-31 Air Products And Chemicals, Inc. Process for removal of carbon dioxide from mixtures containing carbon dioxide and methane
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
US5044932A (en) 1989-10-19 1991-09-03 It-Mcgill Pollution Control Systems, Inc. Nitrogen oxide control using internally recirculated flue gas
US5135387A (en) 1989-10-19 1992-08-04 It-Mcgill Environmental 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
US5098282A (en) 1990-09-07 1992-03-24 John Zink Company Methods and apparatus for burning fuel with low NOx formation
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
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
US5133406A (en) * 1991-07-05 1992-07-28 Amoco Corporation Generating oxygen-depleted air useful for increasing methane production
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
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
US5628182A (en) 1993-07-07 1997-05-13 Mowill; R. Jan Star combustor with dilution ports in can portions
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
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
US5363913A (en) * 1993-08-30 1994-11-15 Phillips Petroleum Company Injection of sequestering agents for subterranean microbial processes
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
CN1052053C (zh) 1993-12-10 2000-05-03 卡伯特公司 一种改进的以液化天然气为燃料的联合循环发电设备
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
EP0828929B1 (en) 1994-08-25 2004-09-22 Clean Energy Systems, Inc. Reduced pollution power generation system and gas generator therefore
US5484019A (en) * 1994-11-21 1996-01-16 Halliburton Company Method for cementing in a formation subject to water influx
US5640840A (en) 1994-12-12 1997-06-24 Westinghouse Electric Corporation Recuperative steam cooled gas turbine method and apparatus
US5836164A (en) 1995-01-30 1998-11-17 Hitachi, Ltd. Gas turbine combustor
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
DE69625744T2 (de) 1995-06-05 2003-10-16 Rolls Royce Corp Magervormischbrenner mit niedrigem NOx-Ausstoss für industrielle Gasturbinen
US6170264B1 (en) 1997-09-22 2001-01-09 Clean Energy Systems, Inc. Hydrocarbon combustion power generation system with CO2 sequestration
US5680764A (en) 1995-06-07 1997-10-28 Clean Energy Systems, Inc. Clean air engines transportation and other power applications
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
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
ATE191254T1 (de) 1995-12-27 2000-04-15 Shell Int Research Flamenlose verbrennvorrichtung und verfahren
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
US5771868A (en) 1997-07-03 1998-06-30 Turbodyne Systems, Inc. Turbocharging systems for internal combustion engines
US5771867A (en) 1997-07-03 1998-06-30 Caterpillar Inc. Control system for exhaust gas recovery system in an internal combustion engine
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
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
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
EP0994243B1 (en) 1998-10-14 2005-01-26 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
US6186228B1 (en) * 1998-12-01 2001-02-13 Phillips Petroleum Company Methods and apparatus for enhancing well production using sonic energy
NO308401B1 (no) 1998-12-04 2000-09-11 Norsk Hydro As FremgangsmÕte for gjenvinning av CO2 som genereres i en forbrenningsprosess samt anvendelse derav
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
DE19857234C2 (de) 1998-12-11 2000-09-28 Daimler Chrysler Ag Vorrichtung zur Abgasrückführung
US6306917B1 (en) * 1998-12-16 2001-10-23 Rentech, Inc. Processes for the production of hydrocarbons, power and carbon dioxide from carbon-containing materials
WO2000040851A1 (en) 1999-01-04 2000-07-13 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
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
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
EP1208293A4 (en) 1999-07-22 2005-10-05 Bechtel Corp METHOD AND APPARATUS FOR VAPORIZING A LIQUID 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
US6298654B1 (en) 1999-09-07 2001-10-09 VERMES GéZA 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
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
WO2001090548A1 (en) 2000-05-12 2001-11-29 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
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
DE60227355D1 (de) * 2001-03-15 2008-08-14 Alexei Leonidovich Zapadinski Verfahren zum entwickeln einer kohlenwasserstoff-lagerstätte sowie anlagenkomplex zur ausführung des verfahrens
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
US6745573B2 (en) 2001-03-23 2004-06-08 American Air Liquide, Inc. Integrated air separation and power generation process
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
AU2002303481A1 (en) 2001-04-24 2002-11-05 Shell Oil Company In situ recovery from a relatively low permeability formation containing heavy hydrocarbons
WO2002085821A2 (en) 2001-04-24 2002-10-31 Shell International Research Maatschappij B.V. In situ recovery from a relatively permeable formation containing heavy hydrocarbons
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
US6923915B2 (en) 2001-08-30 2005-08-02 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
US20030221409A1 (en) 2002-05-29 2003-12-04 Mcgowan Thomas F. Pollution reduction fuel efficient combustion turbine
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
DE50207526D1 (de) 2001-10-01 2006-08-24 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
WO2003036033A1 (en) * 2001-10-24 2003-05-01 Shell Internationale Research Maatschappij B.V. Simulation of in situ recovery from a hydrocarbon containing formation
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
GB2399600B (en) 2001-10-26 2005-12-14 Alstom Technology Ltd Gas turbine adapted to operate with a high exhaust gas recirculation rate and a method for operation thereof
CA2465384C (en) 2001-11-09 2008-09-09 Kawasaki Jukogyo Kabushiki Kaisha Gas turbine system comprising closed system of fuel and combustion gas using underground coal bed
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
EP1362984B1 (en) 2002-05-16 2007-04-25 ROLLS-ROYCE plc Gas turbine engine
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
WO2004042200A1 (en) 2002-11-08 2004-05-21 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
AU2003295681A1 (en) 2002-11-15 2004-06-15 Catalytica Energy Systems, Inc. Devices and methods for reduction of nox emissions from lean burn engines
GB0226983D0 (en) 2002-11-19 2002-12-24 Boc Group Plc Nitrogen rejection method and apparatus
NO320939B1 (no) * 2002-12-10 2006-02-13 Aker Kvaerner Engineering & Te Fremgangsmate for eksosgassbehandling i brenselcellesystem basert pa oksider i fast form
DE10257704A1 (de) 2002-12-11 2004-07-15 Alstom Technology Ltd Verfahren zur Verbrennung eines Brennstoffs
NO20026021D0 (no) * 2002-12-13 2002-12-13 Statoil Asa I & K Ir Pat Fremgangsmåte for ökt oljeutvinning
AU2002351515A1 (en) * 2002-12-13 2004-07-09 Petrosa (The Petroleum Oil & Gas Corporation Of Sa (Pty) Ltd A method for oil recovery from an oil field
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
JP2006515659A (ja) 2003-01-17 2006-06-01 カタリティカ エナジー システムズ， インコーポレイテッド 複数燃焼室触媒ガスタービンエンジンのための動的制御システムおよび方法
US8631657B2 (en) 2003-01-22 2014-01-21 Vast Power Portfolio, Llc Thermodynamic cycles with thermal diluent
US7523603B2 (en) 2003-01-22 2009-04-28 Vast Power Portfolio, Llc Trifluid reactor
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
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
US7053128B2 (en) 2003-02-28 2006-05-30 Exxonmobil Research And Engineering Company Hydrocarbon synthesis process using pressure swing reforming
US7914764B2 (en) 2003-02-28 2011-03-29 Exxonmobil Research And Engineering Company 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
US7513099B2 (en) 2003-03-28 2009-04-07 Siemens Aktiengesellschaft Temperature measuring device and regulation of the temperature of hot gas of a gas turbine
AU2003222696A1 (en) 2003-04-29 2004-11-23 Consejo Superior De Investigaciones Cientificas 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
NO20033230D0 (no) * 2003-07-16 2003-07-16 Statoil Asa Fremgangsmåte for utvinning og oppgradering av olje
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
US20060230935A1 (en) * 2004-03-23 2006-10-19 Keith Michael Method and system for producing inert gas from combustion by-products
US20060000357A1 (en) * 2004-03-23 2006-01-05 Keith Michael Method and system for producing inert gas from combustion by-products
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
WO2005095863A1 (de) 2004-03-31 2005-10-13 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
US7934926B2 (en) 2004-05-06 2011-05-03 Deka Products Limited Partnership 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
WO2005123237A2 (en) 2004-05-14 2005-12-29 Eco/Technologies, Llc Method and system for sequestering carbon emissions from a combustor/boiler
WO2005119029A1 (en) 2004-05-19 2005-12-15 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
WO2005124231A2 (en) 2004-06-11 2005-12-29 Vast Power Systems, Inc. Low emissions combustion apparatus and method
WO2006046976A2 (en) 2004-06-14 2006-05-04 University Of Florida Research Foundation, Inc. Turbine system with exhaust gas recirculation and absorption refrigeration system
EA009276B1 (ru) 2004-07-14 2007-12-28 Флуор Текнолоджиз Корпорейшн Конструкции и способы для выработки электроэнергии с регазификацией сжиженного природного газа
DE102004039164A1 (de) 2004-08-11 2006-03-02 Alstom Technology Ltd Verfahren zur Erzeugung von Energie in einer eine Gasturbine umfassenden Energieerzeugungsanlage sowie Energieerzeugungsanlage zur Durchführung des Verfahrens
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
KR101178431B1 (ko) 2004-09-29 2012-08-31 다이헤이요 세멘토 가부시키가이샤 시멘트 킬른 연소가스 추기 더스트의 처리 시스템 및 처리방법
DK1795510T3 (da) 2004-09-29 2014-06-16 Taiheiyo Cement Corp System og fremgangsmåde til behandling af gasstøv udtaget fra cementovnsforbrændingsgas
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
PL1681090T3 (pl) 2005-01-17 2007-10-31 Balcke Duerr Gmbh Urządzenie i sposób mieszania strumienia płynu w kanale przepływowym
US20060183009A1 (en) 2005-02-11 2006-08-17 Berlowitz Paul J Fuel cell fuel processor with hydrogen buffering
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
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
MX2007011840A (es) 2005-03-30 2007-11-22 Fluor Tech Corp Configuraciones y metodos para integracion termica de regasificacion de gas natural licuado y plantas de energia.
US8316665B2 (en) 2005-03-30 2012-11-27 Fluor Technologies Corporation Integration of LNG regasification with refinery and power generation
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
WO2006107209A1 (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
CA2505449C (en) * 2005-04-27 2007-03-13 Steve Kresnyak Flue gas injection for heavy oil recovery
US8262343B2 (en) 2005-05-02 2012-09-11 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
US7481048B2 (en) 2005-06-30 2009-01-27 Caterpillar Inc. Regeneration assembly
US7966822B2 (en) 2005-06-30 2011-06-28 General Electric Company Reverse-flow gas turbine combustion system
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
CA2616262C (en) * 2005-07-19 2013-07-02 Pacific Consolidated Industries, Llc Mobile nitrogen generation device
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
EP1941127A1 (en) * 2005-10-24 2008-07-09 Shell Oil Company Systems and methods for producing hydrocarbons from tar sands with heat created drainage paths
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
KR101333141B1 (ko) 2005-11-07 2013-11-26 스페셜리스트 프로세스 테크놀로지스 리미티드 기능성 유체 및 기능성 유체를 제조하기 위한 공정
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
US7896105B2 (en) 2005-11-18 2011-03-01 Exxonmobil Upstream Research Company Method of drilling and production hydrocarbons from subsurface formations
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
CN101331081A (zh) 2005-12-16 2008-12-24 国际壳牌研究有限公司 冷却热烟气流的方法
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
CA2645450A1 (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
AU2007262669A1 (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
BRPI0713299A2 (pt) 2006-07-07 2012-04-17 Shell Int Research processo para a fabricação de dissulfeto de carbono, e, uso de uma corrente lìquida
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
US7644611B2 (en) * 2006-09-15 2010-01-12 Schlumberger Technology Corporation Downhole fluid analysis for production logging
BRPI0716921A2 (pt) 2006-09-18 2013-11-12 Shell Int Research Processo para a fabricação de dissulfeto de carbono
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
GB0620883D0 (en) 2006-10-20 2006-11-29 Johnson Matthey Plc Exhaust system for a lean-burn internal combustion engine
US7566394B2 (en) 2006-10-20 2009-07-28 Saudi Arabian Oil Company Enhanced solvent deasphalting process for heavy hydrocarbon feedstocks utilizing solid adsorbent
US7763163B2 (en) 2006-10-20 2010-07-27 Saudi Arabian Oil Company Process for removal of nitrogen and poly-nuclear aromatics from hydrocracker feedstocks
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
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
US7895822B2 (en) 2006-11-07 2011-03-01 General Electric Company Systems and methods for power generation with carbon dioxide isolation
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
EP1944268A1 (en) 2006-12-18 2008-07-16 BP Alternative Energy Holdings Limited Process
US7802434B2 (en) 2006-12-18 2010-09-28 General Electric Company Systems and processes for reducing NOx emissions
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
FR2911667B1 (fr) 2007-01-23 2009-10-02 Snecma Sa Systeme d'injection de carburant a double injecteur.
US7819951B2 (en) 2007-01-23 2010-10-26 Air Products And Chemicals, Inc. Purification of carbon dioxide
WO2008090168A1 (en) 2007-01-25 2008-07-31 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
AU2008215869B2 (en) 2007-02-12 2011-02-10 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
CA2613873C (en) 2007-05-03 2008-10-28 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
US20080290719A1 (en) 2007-05-25 2008-11-27 Kaminsky Robert D Process for producing Hydrocarbon fluids combining in situ heating, a power plant and a gas plant
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
EP2158388B1 (de) 2007-06-19 2019-09-11 Ansaldo Energia IP UK Limited Gasturbinenanlage mit abgasrezirkulation
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
US20090038247A1 (en) 2007-08-09 2009-02-12 Tapco International Corporation Exterior trim pieces with weather stripping and colored protective layer
US7845406B2 (en) 2007-08-30 2010-12-07 George Nitschke Enhanced oil recovery system for use with a geopressured-geothermal conversion system
AU2008292143B2 (en) 2007-08-30 2011-12-08 Shell Internationale Research Maatschappij B.V. Process for removal of hydrogen sulphide and carbon dioxide from an acid gas stream
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
WO2009077866A2 (en) 2007-10-22 2009-06-25 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
US8220268B2 (en) 2007-11-28 2012-07-17 Caterpillar Inc. Turbine engine having fuel-cooled air intercooling
US20110226010A1 (en) 2007-11-28 2011-09-22 Brigham Young University Carbon dioxide capture from flue gas
EP2067941A3 (de) 2007-12-06 2013-06-26 Alstom Technology Ltd Kombikraftwerk mit Abgasrückführung und CO2-Abscheidung sowie Verfahren zum Betrieb eines solchen Kombikraftwerks
US8133298B2 (en) 2007-12-06 2012-03-13 Air Products And Chemicals, Inc. Blast furnace iron production with integrated power generation
US7536252B1 (en) 2007-12-10 2009-05-19 General Electric Company Method and system for controlling a flowrate of a recirculated exhaust gas
US8046986B2 (en) 2007-12-10 2011-11-01 General Electric Company Method and system for controlling an exhaust gas recirculation system
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
US20090193809A1 (en) 2008-02-04 2009-08-06 Mark Stewart Schroder Method and system to facilitate combined cycle working fluid modification and combustion thereof
WO2009098597A2 (en) 2008-02-06 2009-08-13 Osum Oil Sands Corp. Method of controlling a recovery and upgrading operation in a reservor
CA2715973C (en) 2008-02-12 2014-02-11 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
CA2684817C (en) 2008-12-12 2017-09-12 Maoz Betzer-Zilevitch Steam generation process and system for enhanced oil recovery
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
US7753972B2 (en) 2008-08-17 2010-07-13 Pioneer Energy, Inc Portable apparatus for extracting low carbon petroleum and for generating low carbon electricity
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
US8745978B2 (en) 2008-09-19 2014-06-10 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
SG195533A1 (en) 2008-10-14 2013-12-30 Exxonmobil Upstream Res Co Methods and systems for controlling the products of combustion
US8454350B2 (en) 2008-10-29 2013-06-04 General Electric Company Diluent shroud for combustor
EP2368031B1 (en) 2008-11-24 2019-07-03 Ares Turbine AS Gas turbine with external combustion, applying a rotating regenerating heat exchanger
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
US20100170253A1 (en) 2009-01-07 2010-07-08 General Electric Company Method and apparatus for fuel injection in a turbine engine
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
US8127936B2 (en) 2009-03-27 2012-03-06 Uop Llc High performance cross-linked polybenzoxazole and polybenzothiazole polymer membranes
US8127937B2 (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
SG176670A1 (en) 2009-06-05 2012-01-30 Exxonmobil Upstream Res Co Combustor systems and methods for using same
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
US8436489B2 (en) 2009-06-29 2013-05-07 Lightsail Energy, Inc. Compressed air energy storage system utilizing two-phase flow to facilitate heat exchange
US8196395B2 (en) 2009-06-29 2012-06-12 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
CN102482940A (zh) 2009-09-01 2012-05-30 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
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
EA023673B1 (ru) 2009-11-12 2016-06-30 Эксонмобил Апстрим Рисерч Компани Система и способ для низкоэмиссионного производства электроэнергии и извлечения углеводородов
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
MY156099A (en) 2010-07-02 2016-01-15 Exxonmobil Upstream Res Co Systems and methods for controlling combustion of a fuel
JP5913305B2 (ja) 2010-07-02 2016-04-27 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 低エミッション発電システム及び方法
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
PL2588727T3 (pl) 2010-07-02 2019-05-31 Exxonmobil Upstream Res Co Spalanie stechiometryczne z recyrkulacją gazów spalinowych i chłodnicą bezpośredniego kontaktu
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
BR112012031153A2 (pt) 2010-07-02 2016-11-08 Exxonmobil Upstream Res Co sistemas e métodos de geração de energia de triplo-ciclo de baixa emissão
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
US8627643B2 (en) 2010-08-05 2014-01-14 General Electric Company System and method for measuring temperature within a turbine system
US9019108B2 (en) 2010-08-05 2015-04-28 General Electric Company Thermal measurement system for fault detection within a power generation 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
EP2601393B1 (en) 2010-08-06 2020-01-15 Exxonmobil Upstream Research Company Systems and methods for optimizing stoichiometric combustion
WO2012018458A1 (en) 2010-08-06 2012-02-09 Exxonmobil Upstream Research Company System and method for exhaust gas extraction
US8220248B2 (en) 2010-09-13 2012-07-17 Membrane Technology And Research, Inc Power generation process with partial recycle of carbon dioxide
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)
TWI563166B (en) 2011-03-22 2016-12-21 Exxonmobil Upstream Res Co Integrated generation systems and methods for generating power
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
TWI563165B (en) 2011-03-22 2016-12-21 Exxonmobil Upstream Res Co Power generation system and method for generating power
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
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
EA201391364A1 (ru) 2011-03-22 2014-01-30 Эксонмобил Апстрим Рисерч Компани Система и способы улавливания диоксида углерода в турбинных системах с низким уровнем выбросов загрязняющих веществ
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
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
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
US20120023954A1 (en) 2011-08-25 2012-02-02 General Electric Company Power plant and method of operation
US8205455B2 (en) 2011-08-25 2012-06-26 General Electric Company Power plant and method of operation
US8245493B2 (en) 2011-08-25 2012-08-21 General Electric Company Power plant and control method
US8266913B2 (en) 2011-08-25 2012-09-18 General Electric Company Power plant and method of use
US8713947B2 (en) 2011-08-25 2014-05-06 General Electric Company Power plant with gas separation system
US8453461B2 (en) 2011-08-25 2013-06-04 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
US8347600B2 (en) 2011-08-25 2013-01-08 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
US20130086917A1 (en) 2011-10-06 2013-04-11 Ilya Aleksandrovich Slobodyanskiy Apparatus for head end direct air injection with enhanced mixing capabilities
US9097424B2 (en) 2012-03-12 2015-08-04 General Electric Company System for supplying a fuel and working fluid mixture to a combustor
US20150153044A1 (en) 2012-03-29 2015-06-04 General Electric Company Turbomachine combustor assembly
WO2013147632A1 (en) 2012-03-29 2013-10-03 General Electric Company Bi-directional end cover with extraction capability for gas turbine combustor
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
US8539749B1 (en) 2012-04-12 2013-09-24 General Electric Company Systems and apparatus relating to reheat combustion turbine engines with exhaust gas recirculation
US20130269361A1 (en) 2012-04-12 2013-10-17 General Electric Company Methods relating to reheat combustion turbine engines with exhaust gas recirculation
US20130269360A1 (en) 2012-04-12 2013-10-17 General Electric Company Method and system for controlling a powerplant during low-load operations
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
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
US20130269310A1 (en) 2012-04-12 2013-10-17 General Electric Company Systems and apparatus relating to reheat combustion turbine engines with exhaust gas recirculation
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
US20130269357A1 (en) 2012-04-12 2013-10-17 General Electric Company Method and system for controlling a secondary flow system
AU2013245959B2 (en) 2012-04-12 2016-03-31 Exxonmobil Upstream Research Company System and method for a stoichiometric exhaust gas recirculation gas turbine system
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
CN104736817B (zh) 2012-04-26 2017-10-24 通用电气公司 再循环用于燃气涡轮发动机中多个流动路径中的排气的系统和方法
US20140060073A1 (en) 2012-08-28 2014-03-06 General Electric Company Multiple point overboard extractor for gas turbine
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
US9869279B2 (en) 2012-11-02 2018-01-16 General Electric Company System and method for a multi-wall 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
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
WO2014071118A1 (en) 2012-11-02 2014-05-08 General Electric Company System and method for reheat in gas turbine with exhaust gas recirculation
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
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

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4434613A (en) * 1981-09-02 1984-03-06 General Electric Company Closed cycle gas turbine for gaseous production
CN1451844A (zh) * 2003-05-09 2003-10-29 辽河石油勘探局 一种油田开采热、电、co2、n2联供制造方法

Also Published As

Publication number Publication date
CN101981272A (zh) 2011-02-23
CA2934541C (en) 2018-11-06
US20110000221A1 (en) 2011-01-06
EP2268897B1 (en) 2020-11-11
WO2009120779A3 (en) 2010-01-07
CA2934542A1 (en) 2009-10-01
EP2268897A4 (en) 2017-10-18
EP2268897A2 (en) 2011-01-05
CA2715186A1 (en) 2009-10-01
CA2934541A1 (en) 2009-10-01
CA2715186C (en) 2016-09-06
WO2009120779A2 (en) 2009-10-01
AU2009228283B2 (en) 2015-02-05
AU2009228283A1 (en) 2009-10-01
US8984857B2 (en) 2015-03-24
CA2934542C (en) 2018-11-06
MY156350A (en) 2016-02-15

Similar Documents

Publication Publication Date Title
CN101981272B (zh) 低排放发电和烃采收系统及方法
JP6348416B2 (ja) 低エミッションタービンシステムにおいて化学量論的燃焼を制御するシステム及び方法
JP6147725B2 (ja) 低エミッションタービンシステムにおける二酸化炭素捕捉及び動力発生のためのシステム及び方法
JP6099057B2 (ja) 入口圧縮機用酸化剤制御装置を備えた低エミッションタービンシステム及び関連方法
CN101981162B (zh) 低排放发电和烃采收系统及方法
JP5913304B2 (ja) 低エミッショントリプルサイクル発電システム及び方法
CN103953446B (zh) 低排放发电和烃采收系统及方法
TWI564475B (zh) 低排放之三循環動力產生系統和方法
US20080098745A1 (en) Method for obtaining ultra-low NOx emissions from gas turbines operating at high turbine inlet temperatures
CN103442783A (zh) 用于在低排放涡轮机系统中捕获二氧化碳的系统和方法
CN103443403A (zh) 用于在低排放联合涡轮机系统中捕获二氧化碳的系统和方法
EA026404B1 (ru) Интегрированная система и способ производства энергии
CA2439110A1 (en) Integrated air separation and power generation process
MX2012014458A (es) Combustion estequiometrica de aire enriquecido con recirculacion de gas de escape.
CA2306710A1 (en) An advanced technology pollution free, highly efficient industrial power generation system

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20140611

CF01 Termination of patent right due to non-payment of annual fee