WO2007017387A3 - Verfahren zur steigerung des wirkungsgrads eines kombinierten gas- und dampfkraftwerks mit integrierter brennstoffvergasung - Google Patents

Verfahren zur steigerung des wirkungsgrads eines kombinierten gas- und dampfkraftwerks mit integrierter brennstoffvergasung Download PDF

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Publication number
WO2007017387A3
WO2007017387A3 PCT/EP2006/064693 EP2006064693W WO2007017387A3 WO 2007017387 A3 WO2007017387 A3 WO 2007017387A3 EP 2006064693 W EP2006064693 W EP 2006064693W WO 2007017387 A3 WO2007017387 A3 WO 2007017387A3
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WO
WIPO (PCT)
Prior art keywords
air
power station
efficiency
separation unit
steam power
Prior art date
Application number
PCT/EP2006/064693
Other languages
English (en)
French (fr)
Other versions
WO2007017387A2 (de
Inventor
Werner Guenster
Erik Wolf
Gerhard Zimmermann
Original Assignee
Siemens Ag
Werner Guenster
Erik Wolf
Gerhard Zimmermann
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 Siemens Ag, Werner Guenster, Erik Wolf, Gerhard Zimmermann filed Critical Siemens Ag
Priority to CN200680037156.0A priority Critical patent/CN101287893B/zh
Priority to US11/990,034 priority patent/US8020388B2/en
Priority to EP06792578A priority patent/EP1913238A2/de
Publication of WO2007017387A2 publication Critical patent/WO2007017387A2/de
Priority to IL189153A priority patent/IL189153A0/en
Publication of WO2007017387A3 publication Critical patent/WO2007017387A3/de

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K23/00Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
    • F01K23/02Plants 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
    • F01K23/06Plants 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
    • F01K23/067Plants 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
    • F01K23/068Plants 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes 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
    • F25J3/04Processes 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
    • F25J3/04521Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04527Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general
    • F25J3/04539Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general for the H2/CO synthesis by partial oxidation or oxygen consuming reforming processes of fuels
    • F25J3/04545Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general for the H2/CO synthesis by partial oxidation or oxygen consuming reforming processes of fuels for the gasification of solid or heavy liquid fuels, e.g. integrated gasification combined cycle [IGCC]
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes 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
    • F25J3/04Processes 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
    • F25J3/04521Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04563Integration with a nitrogen consuming unit, e.g. for purging, inerting, cooling or heating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes 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
    • F25J3/04Processes 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
    • F25J3/04521Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04563Integration with a nitrogen consuming unit, e.g. for purging, inerting, cooling or heating
    • F25J3/04575Integration with a nitrogen consuming unit, e.g. for purging, inerting, cooling or heating for a gas expansion plant, e.g. dilution of the combustion gas in a gas turbine
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes 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
    • F25J3/04Processes 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
    • F25J3/04521Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04563Integration with a nitrogen consuming unit, e.g. for purging, inerting, cooling or heating
    • F25J3/04575Integration with a nitrogen consuming unit, e.g. for purging, inerting, cooling or heating for a gas expansion plant, e.g. dilution of the combustion gas in a gas turbine
    • F25J3/04581Hot gas expansion of indirect heated nitrogen
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes 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
    • F25J3/04Processes 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
    • F25J3/04521Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04593The air gas consuming unit is also fed by an air stream
    • F25J3/04606Partially integrated air feed compression, i.e. independent MAC for the air fractionation unit plus additional air feed from the air gas consuming unit
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes 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
    • F25J3/04Processes 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
    • F25J3/04521Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04612Heat exchange integration with process streams, e.g. from the air gas consuming unit
    • F25J3/04618Heat exchange integration with process streams, e.g. from the air gas consuming unit for cooling an air stream fed to the air fractionation unit
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2210/00Processes characterised by the type or other details of the feed stream
    • F25J2210/04Mixing or blending of fluids with the feed stream
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2240/00Processes or apparatus involving steps for expanding of process streams
    • F25J2240/70Steam turbine, e.g. used in a Rankine cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2240/00Processes or apparatus involving steps for expanding of process streams
    • F25J2240/80Hot exhaust gas turbine combustion engine
    • F25J2240/82Hot exhaust gas turbine combustion engine with waste heat recovery, e.g. in a combined cycle, i.e. for generating steam used in a Rankine cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2245/00Processes or apparatus involving steps for recycling of process streams
    • F25J2245/42Processes or apparatus involving steps for recycling of process streams the recycled stream being nitrogen
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2260/00Coupling of processes or apparatus to other units; Integrated schemes
    • F25J2260/42Integration in an installation using nitrogen, e.g. as utility gas, for inerting or purging purposes in IGCC, POX, GTL, PSA, float glass forming, incineration processes, for heat recovery or for enhanced oil recovery
    • F25J2260/44Integration in an installation using nitrogen, e.g. as utility gas, for inerting or purging purposes in IGCC, POX, GTL, PSA, float glass forming, incineration processes, for heat recovery or for enhanced oil recovery using nitrogen for cooling purposes
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/16Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/16Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
    • Y02E20/18Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Power Engineering (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Abstract

Die Erfindung betrifft ein Verfahren zur Steigerung des Wirkungsgrads eines kombinierten Gas- und Dampfkraftwerks (10) mit integrierter Brennstoffvergasung, das einen Gasturbinen-Verdichter (14) und eine Luftzerlegungsanlage (18) mit einem vorgegebenen Betriebsdruck aufweist, bei dem verdichtete Luft aus dem Gasturbinen-Verdichter (14) auf einem Druckniveau entnommen wird, welches dem Betriebsdruck der Luftzerlegungsanlage (18) angepasst ist, die entnommene Luft anschließend der Luftzerlegungsanlage (18) zugeführt wird, in welcher die Luft in ihre einzelnen Bestandteile, insbesondere in Sauerstoff und Stickstoff zerlegt wird, der in der Luftzerlegungsanlage (18) erzeugte Stickstoff aus der Luftzerlegungsanlage (18) entnommen wird, und zumindest ein Teil der entnommenen Stickstoffmenge als Kühlmedium am Gas- und Dampfkraftwerk verwendet wird, um dessen Wirkungsgrad zu steigern .
PCT/EP2006/064693 2005-08-05 2006-07-26 Verfahren zur steigerung des wirkungsgrads eines kombinierten gas- und dampfkraftwerks mit integrierter brennstoffvergasung WO2007017387A2 (de)

Priority Applications (4)

Application Number Priority Date Filing Date Title
CN200680037156.0A CN101287893B (zh) 2005-08-05 2006-07-26 提高带有一体化燃料气化器的燃气和蒸汽联合发电厂效率的方法
US11/990,034 US8020388B2 (en) 2005-08-05 2006-07-26 Method for increasing the efficiency of a combined gas/steam power station with integrated gasification combined cycle
EP06792578A EP1913238A2 (de) 2005-08-05 2006-07-26 Verfahren zur steigerung des wirkungsgrads eines kombinierten gas- und dampfkraftwerks mit integrierter brennstoffvergasung
IL189153A IL189153A0 (en) 2005-08-05 2008-01-31 Method for increasing the efficiency of a combined gas/steam power station with integrated gasification combined cycle

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP05017062.0 2005-08-05
EP05017062 2005-08-05

Publications (2)

Publication Number Publication Date
WO2007017387A2 WO2007017387A2 (de) 2007-02-15
WO2007017387A3 true WO2007017387A3 (de) 2008-07-03

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PCT/EP2006/064693 WO2007017387A2 (de) 2005-08-05 2006-07-26 Verfahren zur steigerung des wirkungsgrads eines kombinierten gas- und dampfkraftwerks mit integrierter brennstoffvergasung

Country Status (5)

Country Link
US (1) US8020388B2 (de)
EP (1) EP1913238A2 (de)
CN (1) CN101287893B (de)
IL (1) IL189153A0 (de)
WO (1) WO2007017387A2 (de)

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US8020397B2 (en) * 2008-10-30 2011-09-20 General Electric Company Reduction of diluent nitrogen compressor power using vapor absorption chiller
US8069672B2 (en) * 2008-12-22 2011-12-06 General Electric Company Method and systems for operating a combined cycle power plant
US20100186367A1 (en) * 2009-01-27 2010-07-29 General Electric Company Gas turbine with introduction of nitrogen
EP2256317A1 (de) * 2009-05-29 2010-12-01 Shell Internationale Research Maatschappij B.V. Verfahren zur Krafterzeugung
US8529679B2 (en) 2009-11-05 2013-09-10 General Electric Company System and method for improving performance of an IGCC power plant
US8186169B2 (en) * 2010-10-22 2012-05-29 General Electric Company Nitrogen cooled gas turbine with combustor nitrogen injection and partial nitrogen recycling
AT12844U1 (de) * 2011-12-28 2012-12-15 Ge Jenbacher Gmbh & Co Ohg Verfahren zum Betreiben einer stationären Kraftanlage mit wenigstens einer Brennkraftmaschine
US9003796B2 (en) * 2012-06-05 2015-04-14 General Electric Company Heat recovery using organic rankine cycle
US20140020426A1 (en) * 2012-07-17 2014-01-23 General Electric Company System and method for using a chilled fluid to cool an electromechanical machine
US20140130509A1 (en) * 2012-11-13 2014-05-15 Raymond Francis Drnevich Combined gasification and power generation
RU2524317C1 (ru) * 2013-03-27 2014-07-27 Геннадий Павлович Барчан Способ преобразования энергии с регенерацией энергоносителей в циклическом процессе теплового двигателя
CN105673098A (zh) * 2016-03-02 2016-06-15 青岛捷能高新技术有限责任公司 侧向排气偏心凝汽系统及方法
EP3333123B1 (de) * 2016-12-09 2019-11-27 L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude Verfahren und anlage zur erzeugung von synthesegas
CN109252842B (zh) * 2018-10-29 2024-04-12 邓晓亮 超临界煤炭地下气化产出混合气体三联供发电系统
CN109441574B (zh) * 2018-11-02 2021-07-23 中国石油大学(华东) 用于调峰的近零碳排放整体煤气化联合发电工艺
CN109441573B (zh) * 2018-11-02 2021-07-23 中国石油大学(华东) 用于调峰的零碳排放天然气联合发电工艺
CN109812335B (zh) * 2019-01-15 2021-11-16 中国石油大学(华东) 零碳排放的整体煤气化-蒸气联合循环发电工艺
CN109578098A (zh) * 2019-01-15 2019-04-05 中国石油大学(华东) 零碳排放的天然气热电联供发电工艺
CN109611171A (zh) * 2019-01-15 2019-04-12 中国石油大学(华东) 零碳排放的整体煤气化-超临界co2联合循环发电工艺
CN109609199B (zh) * 2019-01-15 2020-07-21 中国石油大学(华东) 零碳排放的煤气化热电联供工艺

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DE19940763A1 (de) * 1998-08-28 2000-03-02 Toshiba Kawasaki Kk Im kombinierten Zyklus arbeitender Energieerzeuger mit integrierter Kohlevergasung

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US5437150A (en) * 1991-05-23 1995-08-01 The Boc Group, Plc Fluid production method and apparatus
EP0634562A2 (de) * 1993-07-16 1995-01-18 Air Products And Chemicals, Inc. Gasturbinenverfahren zur Energiegewinnung mit integrierter Lufttrennungsanlage
JPH0814062A (ja) * 1994-06-28 1996-01-16 Mitsubishi Heavy Ind Ltd 複合発電プラント
JPH08218891A (ja) * 1995-02-09 1996-08-27 Hitachi Ltd ガス化発電プラント
DE19940763A1 (de) * 1998-08-28 2000-03-02 Toshiba Kawasaki Kk Im kombinierten Zyklus arbeitender Energieerzeuger mit integrierter Kohlevergasung

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CN101287893B (zh) 2012-06-13
US20100146929A1 (en) 2010-06-17
EP1913238A2 (de) 2008-04-23
CN101287893A (zh) 2008-10-15
US8020388B2 (en) 2011-09-20
WO2007017387A2 (de) 2007-02-15
IL189153A0 (en) 2009-08-03

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