FR2924203B1 - Adaptation d'une centrale a oxycombustion a la disponibilite de l'energie et a la quantite de co2 a capturer - Google Patents

Adaptation d'une centrale a oxycombustion a la disponibilite de l'energie et a la quantite de co2 a capturer

Info

Publication number
FR2924203B1
FR2924203B1 FR0759319A FR0759319A FR2924203B1 FR 2924203 B1 FR2924203 B1 FR 2924203B1 FR 0759319 A FR0759319 A FR 0759319A FR 0759319 A FR0759319 A FR 0759319A FR 2924203 B1 FR2924203 B1 FR 2924203B1
Authority
FR
France
Prior art keywords
air
unit
capturate
adaptation
availability
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
FR0759319A
Other languages
English (en)
Other versions
FR2924203A1 (fr
Inventor
Philippe Court
Arthur Darde
Jean Pierre Tranier
Bot Patrick Le
Jean Pierre Tsevery
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.)
Air Liquide SA
LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
Original Assignee
Air Liquide SA
LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
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
Priority to FR0759319A priority Critical patent/FR2924203B1/fr
Application filed by Air Liquide SA, LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude filed Critical Air Liquide SA
Priority to CN2008801178466A priority patent/CN101874181B/zh
Priority to CA2704507A priority patent/CA2704507A1/fr
Priority to US12/743,953 priority patent/US8973567B2/en
Priority to AU2008333010A priority patent/AU2008333010B2/en
Priority to EP08857563A priority patent/EP2212621A2/fr
Priority to JP2010534531A priority patent/JP5634872B2/ja
Priority to PCT/FR2008/052121 priority patent/WO2009071833A2/fr
Publication of FR2924203A1 publication Critical patent/FR2924203A1/fr
Application granted granted Critical
Publication of FR2924203B1 publication Critical patent/FR2924203B1/fr
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L7/00—Supplying non-combustible liquids or gases, other than air, to the fire, e.g. oxygen, steam
    • F23L7/007—Supplying oxygen or oxygen-enriched air
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/06—Arrangements of devices for treating smoke or fumes of coolers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04472—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using the cold from cryogenic liquids produced within the air fractionation unit and stored in internal or intermediate storages
    • F25J3/04496—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using the cold from cryogenic liquids produced within the air fractionation unit and stored in internal or intermediate storages for compensating variable air feed or variable product demand by alternating between periods of liquid storage and liquid assist
    • F25J3/04503—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using the cold from cryogenic liquids produced within the air fractionation unit and stored in internal or intermediate storages for compensating variable air feed or variable product demand by alternating between periods of liquid storage and liquid assist by exchanging "cold" between at least two different cryogenic liquids, e.g. independently from the main heat exchange line of the air fractionation and/or by using external alternating storage systems
    • F25J3/04509—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using the cold from cryogenic liquids produced within the air fractionation unit and stored in internal or intermediate storages for compensating variable air feed or variable product demand by alternating between periods of liquid storage and liquid assist by exchanging "cold" between at least two different cryogenic liquids, e.g. independently from the main heat exchange line of the air fractionation and/or by using external alternating storage systems within the cold part of the air fractionation, i.e. exchanging "cold" within the fractionation and/or main heat exchange line
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04472—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using the cold from cryogenic liquids produced within the air fractionation unit and stored in internal or intermediate storages
    • F25J3/04496—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using the cold from cryogenic liquids produced within the air fractionation unit and stored in internal or intermediate storages for compensating variable air feed or variable product demand by alternating between periods of liquid storage and liquid assist
    • F25J3/04503—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using the cold from cryogenic liquids produced within the air fractionation unit and stored in internal or intermediate storages for compensating variable air feed or variable product demand by alternating between periods of liquid storage and liquid assist by exchanging "cold" between at least two different cryogenic liquids, e.g. independently from the main heat exchange line of the air fractionation and/or by using external alternating storage systems
    • F25J3/04509—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using the cold from cryogenic liquids produced within the air fractionation unit and stored in internal or intermediate storages for compensating variable air feed or variable product demand by alternating between periods of liquid storage and liquid assist by exchanging "cold" between at least two different cryogenic liquids, e.g. independently from the main heat exchange line of the air fractionation and/or by using external alternating storage systems within the cold part of the air fractionation, i.e. exchanging "cold" within the fractionation and/or main heat exchange line
    • F25J3/04515—Simultaneously changing air feed and products output
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04521—Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04527—Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general
    • F25J3/04533—Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general for the direct combustion of fuels in a power plant, so-called "oxyfuel combustion"
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/50—Carbon oxides
    • B01D2257/504—Carbon dioxide
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2215/00—Preventing emissions
    • F23J2215/50—Carbon dioxide
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2900/00—Special arrangements for conducting or purifying combustion fumes; Treatment of fumes or ashes
    • F23J2900/15061—Deep cooling or freezing of flue gas rich of CO2 to deliver CO2-free emissions, or to deliver liquid CO2
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L2900/00—Special arrangements for supplying or treating air or oxidant for combustion; Injecting inert gas, water or steam into the combustion chamber
    • F23L2900/07001—Injecting synthetic air, i.e. a combustion supporting mixture made of pure oxygen and an inert gas, e.g. nitrogen or recycled fumes
    • 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
    • Y02E20/30—Technologies for a more efficient combustion or heat usage
    • 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
    • Y02E20/32—Direct CO2 mitigation
    • 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

Abstract

Procédé de combustion de combustibles carbonés mettant en oeuvre une unité de séparation des gaz de l'air, une unité de combustion fonctionnant soit à l'air, soit à un comburant plus pauvre en azote que l'air, au moins partiellement issu de l'unité de séparation des gaz de l'air , et une unité de compression et/ou de purification du CO2 issu des fumées de combustion, caractérisé en ce que pendant une durée T finie:- la puissance appelée par l'unité de séparation des gaz de l'air est variable, et/ou- la capture du CO2 issu des fumées de combustion, via l'unité de compression et/ou de purification du CO2, est variable.
FR0759319A 2007-11-26 2007-11-26 Adaptation d'une centrale a oxycombustion a la disponibilite de l'energie et a la quantite de co2 a capturer Expired - Fee Related FR2924203B1 (fr)

Priority Applications (8)

Application Number Priority Date Filing Date Title
FR0759319A FR2924203B1 (fr) 2007-11-26 2007-11-26 Adaptation d'une centrale a oxycombustion a la disponibilite de l'energie et a la quantite de co2 a capturer
CA2704507A CA2704507A1 (fr) 2007-11-26 2008-11-25 Adaptation d'une centrale a oxycombustion a la disponibilite de l'energie et a la quantite de co2 a capturer
US12/743,953 US8973567B2 (en) 2007-11-26 2008-11-25 Adapting of an oxy-combustion plant to energy availability and to the amount of CO2 to be trapped
AU2008333010A AU2008333010B2 (en) 2007-11-26 2008-11-25 Adapting of an oxy-combustion plant to energy availability and to the amount of CO2 to be trapped
CN2008801178466A CN101874181B (zh) 2007-11-26 2008-11-25 氧燃烧厂与可获得的能量及待收集的co2量的适配
EP08857563A EP2212621A2 (fr) 2007-11-26 2008-11-25 Adaptation d'une centrale a oxycombustion a la disponibilite de l'energie et a la quantite de co2 a capturer
JP2010534531A JP5634872B2 (ja) 2007-11-26 2008-11-25 炭素燃料燃焼方法
PCT/FR2008/052121 WO2009071833A2 (fr) 2007-11-26 2008-11-25 Adaptation d'une centrale a oxycombustion a la disponibilite de l'energie et a la quantite de co2 a capturer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR0759319A FR2924203B1 (fr) 2007-11-26 2007-11-26 Adaptation d'une centrale a oxycombustion a la disponibilite de l'energie et a la quantite de co2 a capturer

Publications (2)

Publication Number Publication Date
FR2924203A1 FR2924203A1 (fr) 2009-05-29
FR2924203B1 true FR2924203B1 (fr) 2010-04-02

Family

ID=39627725

Family Applications (1)

Application Number Title Priority Date Filing Date
FR0759319A Expired - Fee Related FR2924203B1 (fr) 2007-11-26 2007-11-26 Adaptation d'une centrale a oxycombustion a la disponibilite de l'energie et a la quantite de co2 a capturer

Country Status (8)

Country Link
US (1) US8973567B2 (fr)
EP (1) EP2212621A2 (fr)
JP (1) JP5634872B2 (fr)
CN (1) CN101874181B (fr)
AU (1) AU2008333010B2 (fr)
CA (1) CA2704507A1 (fr)
FR (1) FR2924203B1 (fr)
WO (1) WO2009071833A2 (fr)

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2949845B1 (fr) * 2009-09-09 2011-12-02 Air Liquide Procede d'operation d'au moins un appareil de separation d'air et d'une unite de combustion de combustibles carbones
JP4896195B2 (ja) * 2009-09-30 2012-03-14 株式会社日立製作所 酸素燃焼ボイラプラント及び酸素燃焼ボイラプラントの運転方法
US8550810B2 (en) * 2010-05-28 2013-10-08 Foster Wheeler North America Corp. Method of controlling a boiler plant during switchover from air-combustion to oxygen-combustion
GB201021480D0 (en) * 2010-12-17 2011-02-02 Doosan Power Systems Ltd Control system and method for power plant
US20120227964A1 (en) * 2011-03-07 2012-09-13 Conocophillips Company Carbon dioxide gas mixture processing with steam assisted oil recovery
CN103234198B (zh) * 2013-04-19 2015-10-28 上海交通大学 超细煤粉富氧燃烧工艺及系统
US9409120B2 (en) 2014-01-07 2016-08-09 The University Of Kentucky Research Foundation Hybrid process using a membrane to enrich flue gas CO2 with a solvent-based post-combustion CO2 capture system
CN105889947A (zh) * 2016-05-30 2016-08-24 广东上典环境保护工程有限公司 一种新型锅炉无硝燃烧系统
CN105889969A (zh) * 2016-05-30 2016-08-24 广东上典环境保护工程有限公司 一种可对二氧化碳进行回收的无硝燃烧系统
KR102074990B1 (ko) * 2018-06-19 2020-02-10 한국생산기술연구원 바이오촤를 이용한 가압순산소 오염물질 포집 시스템
CN210367457U (zh) * 2019-06-28 2020-04-21 江苏中圣园科技股份有限公司 一种以天燃气为燃料的套筒窑
EP3994233A1 (fr) 2019-07-02 2022-05-11 TotalEnergies SE Extraction d'hydrocarbures à l'aide d'énergie solaire
FR3119226B1 (fr) 2021-01-25 2023-05-26 Lair Liquide Sa Pour Letude Et Lexploitation De Procede et appareil de separation d’air par distillation cryogenique
CN113797700A (zh) * 2021-09-22 2021-12-17 乔治洛德方法研究和开发液化空气有限公司 分离空气以及产生富二氧化碳产品的集成单元及方法

Family Cites Families (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05340266A (ja) * 1992-06-09 1993-12-21 Mitsubishi Heavy Ind Ltd 発電方法
JPH0699034A (ja) * 1992-09-21 1994-04-12 Chubu Electric Power Co Inc 燃焼排ガスからの二酸化炭素の液化分離回収法
DE4436904A1 (de) * 1994-10-15 1996-04-18 Kurt Lange Nutzung von Überschuß- und Verlustenergie vorzugsweise in einem gasbetriebenen Motorblockheizkraftwerk zur Primärenergieeinsparung und Umweltentlastung durch Integration eines alkalischen Elektrolyseurs zur Zersetzung von Wasser in Wasserstoff und Sauerstoff
JP3667875B2 (ja) * 1996-05-28 2005-07-06 大陽日酸株式会社 空気液化分離方法
US6401633B2 (en) * 1998-04-06 2002-06-11 Minergy Corporation Closed cycle waste combustion
JP2003126681A (ja) * 2001-10-24 2003-05-07 Yoshisuke Takiguchi 二酸化炭素のエネルギー担体化とその利用法
US6568185B1 (en) * 2001-12-03 2003-05-27 L'air Liquide Societe Anonyme A'directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude Combination air separation and steam-generation processes and plants therefore
US7062912B2 (en) * 2002-02-25 2006-06-20 American Air Liquide, Inc. Integrated heat recovery systems and methods for increasing the efficiency of an oxygen-fired furnace
JP2004041967A (ja) * 2002-07-12 2004-02-12 Toshiba Corp エネルギーシステム
ZA200304880B (en) * 2003-02-24 2004-05-04 Air Liquide Integrated heat recovery systems and methods for increasing the efficiency of an oxygen-fired furnace.
US7228715B2 (en) * 2003-12-23 2007-06-12 L'air Liquide, Societe Anonyme A Directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude Cryogenic air separation process and apparatus
US20060096298A1 (en) * 2004-11-10 2006-05-11 Barnicki Scott D Method for satisfying variable power demand
DE102005012902A1 (de) * 2005-03-21 2006-09-28 Steag Saar Energie Ag Kraftwerksanlage
DE102005026534B4 (de) * 2005-06-08 2012-04-19 Man Diesel & Turbo Se Dampferzeugungsanlage
FR2891609B1 (fr) 2005-10-04 2007-11-23 Inst Francais Du Petrole Procede d'oxy-combustion permettant la capture de la totalite du dioxyde de carbone produit.
JP2007147161A (ja) * 2005-11-28 2007-06-14 Electric Power Dev Co Ltd 燃焼装置の排ガス処分方法及び装置
US20070144415A1 (en) * 2005-11-29 2007-06-28 Varagani Rajani K Coal Upgrading Process Utilizing Nitrogen and/or Carbon Dioxide
US20070251267A1 (en) * 2006-04-26 2007-11-01 Bao Ha Cryogenic Air Separation Process

Also Published As

Publication number Publication date
JP2011505537A (ja) 2011-02-24
EP2212621A2 (fr) 2010-08-04
CN101874181B (zh) 2012-05-23
US20100242811A1 (en) 2010-09-30
CA2704507A1 (fr) 2009-06-11
WO2009071833A3 (fr) 2009-07-30
CN101874181A (zh) 2010-10-27
AU2008333010B2 (en) 2012-11-22
FR2924203A1 (fr) 2009-05-29
WO2009071833A2 (fr) 2009-06-11
AU2008333010A1 (en) 2009-06-11
JP5634872B2 (ja) 2014-12-03
US8973567B2 (en) 2015-03-10

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