WO2014104526A1 - 발전 시스템 - Google Patents
발전 시스템 Download PDFInfo
- Publication number
- WO2014104526A1 WO2014104526A1 PCT/KR2013/007329 KR2013007329W WO2014104526A1 WO 2014104526 A1 WO2014104526 A1 WO 2014104526A1 KR 2013007329 W KR2013007329 W KR 2013007329W WO 2014104526 A1 WO2014104526 A1 WO 2014104526A1
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- WO
- WIPO (PCT)
- Prior art keywords
- fuel cell
- power generation
- cell system
- generation system
- carbon dioxide
- Prior art date
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Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D15/00—Adaptations of machines or engines for special use; Combinations of engines with devices driven thereby
- F01D15/10—Adaptations for driving, or combinations with, electric generators
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C3/00—Gas-turbine plants characterised by the use of combustion products as the working fluid
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
- H01M8/04067—Heat exchange or temperature measuring elements, thermal insulation, e.g. heat pipes, heat pumps, fins
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
- H01M8/04097—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with recycling of the reactants
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0662—Treatment of gaseous reactants or gaseous residues, e.g. cleaning
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0662—Treatment of gaseous reactants or gaseous residues, e.g. cleaning
- H01M8/0668—Removal of carbon monoxide or carbon dioxide
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02K—DYNAMO-ELECTRIC MACHINES
- H02K7/00—Arrangements for handling mechanical energy structurally associated with dynamo-electric machines, e.g. structural association with mechanical driving motors or auxiliary dynamo-electric machines
- H02K7/18—Structural association of electric generators with mechanical driving motors, e.g. with turbines
- H02K7/1807—Rotary generators
- H02K7/1823—Rotary generators structurally associated with turbines or similar engines
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/14—Fuel cells with fused electrolytes
- H01M2008/147—Fuel cells with molten carbonates
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2250/00—Fuel cells for particular applications; Specific features of fuel cell system
- H01M2250/40—Combination of fuel cells with other energy production systems
- H01M2250/402—Combination of fuel cell with other electric generators
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2250/00—Fuel cells for particular applications; Specific features of fuel cell system
- H01M2250/40—Combination of fuel cells with other energy production systems
- H01M2250/405—Cogeneration of heat or hot water
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2250/00—Fuel cells for particular applications; Specific features of fuel cell system
- H01M2250/40—Combination of fuel cells with other energy production systems
- H01M2250/407—Combination of fuel cells with mechanical energy generators
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- 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
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B90/00—Enabling technologies or technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02B90/10—Applications of fuel cells in buildings
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- 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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Definitions
- the present invention relates to a power generation system, and more particularly, to a power generation system according to the present invention, a power generation system for producing power, the power generation system comprising: a fuel cell system for generating power by reacting supplied reactants; And a circulation system for circulating a product produced in the fuel cell system, wherein the circulation system is configured to refeed at least a portion of the product generated in the fuel cell system to a reactant of the fuel cell system.
- a fuel cell is a device that directly converts chemical energy stored in a hydrocarbon fuel into electrical energy by an electrochemical reaction.
- a fuel cell includes an anode pole and a cathode pole separated by an electrolyte that conducts electrically charged ions.
- the molten carbonate fuel cell is operated by passing a reactant fuel gas through an anode pole while oxidizing a gas containing carbon dioxide, and oxygen passes through the cathode pole.
- the present invention has been made to solve the above problems, the power generation system according to the present invention, a power generation system for producing power, the power generation system, a fuel cell system for producing power by reacting the supplied reactant; And a circulation system for circulating a product produced in the fuel cell system, wherein the circulation system is configured to refeed at least a portion of the product generated in the fuel cell system to a reactant of the fuel cell system.
- the power generation system a power generation system for producing electric power, the power generation system, a fuel cell system for producing power by reacting the supplied reactant; And a circulation system for circulating a product produced in the fuel cell system, wherein the circulation system is configured to refeed at least a portion of the product generated in the fuel cell system to a reactant of the fuel cell system.
- the fuel power generation system includes an anode pole, and a cathode pole, to which reactants are reacted, and the anode pole is supplied with hydrogen, and the cathode pole is oxygen and carbon dioxide. Is configured to be supplied.
- the circulation system comprises a separation device for separating at least a portion of the product produced in the fuel cell system and re-supply to the reactants of the fuel cell system.
- the separation device is configured to separate carbon dioxide in the product generated in the fuel cell system and to re-supply it to the fuel cell system.
- the separation device is composed of a phase separation device using the difference in boiling point.
- the combustion system is disposed in the rear of the fuel cell system, by reacting the oxygen and hydrogen contained in the product to generate water and carbon dioxide Is configured to.
- the combustion system is composed of a catalytic combustion system using a predetermined catalyst.
- the power generation system further includes a turbine power generation system including a turbine and generating electric power by rotation of the turbine, wherein the turbine power generation system is located at a rear end of the combustion system. And generate power by rotating the turbine using at least one of water and carbon dioxide produced in the combustion system.
- a turbine power generation system including a turbine and generating electric power by rotation of the turbine, wherein the turbine power generation system is located at a rear end of the combustion system. And generate power by rotating the turbine using at least one of water and carbon dioxide produced in the combustion system.
- it is configured to further include a heat exchange device for exchanging heat and external heat of the product produced in the combustion system.
- the power generation system includes a fuel cell system and a circulation system
- the product produced in the fuel cell system can be reused as a reactant of the fuel cell system. Therefore, the power generation efficiency of the overall power generation system is improved, and it is possible to prevent the discharge of products that can act as a cause of environmental pollution.
- the circulation system recycles carbon dioxide in the product of the fuel cell system, it may contribute to suppressing the generation of pollutants by suppressing the emission of carbon dioxide, which is the cause of global warming.
- the power generation system includes a circulation system including a separation device
- the recycling efficiency of the product generated in the fuel cell may be further increased.
- the carbon dioxide can be separated and reused, thereby contributing to the prevention of environmental pollution.
- the power generation system may be configured as a hybrid power generation system, including a fuel cell system and a turbine power generation system. Accordingly, power generation through a fuel cell and power generation by a turbine using a high-temperature product generated from the fuel cell may be performed together, thereby further improving power output and energy utilization efficiency.
- the power generation system according to an embodiment of the present invention, as the heat exchange device is provided, the overall energy utilization efficiency of the power generation system can be further increased.
- FIG. 1 is a conceptual diagram showing a power generation system according to the present invention.
- FIG. 2 is a view showing a power generation system according to an embodiment of the present invention.
- a power generation system is a power generation system for producing electric power, the power generation system comprising: a fuel cell system for generating electric power by reacting a supplied reactant; And a circulation system for circulating a product produced in the fuel cell system, wherein the circulation system is configured to refeed at least a portion of the product generated in the fuel cell system to a reactant of the fuel cell system.
- FIG. 1 is a conceptual diagram showing a power generation system 1 according to the present invention
- Figure 2 is a view showing a power generation system 1 according to an embodiment of the present invention.
- the power generation system 1 includes a power generation system 1 for generating electric power, comprising: a fuel cell system 100 for producing electric power by reacting reactants; And a circulation system 200 for circulating a product generated in the fuel cell system 100, wherein the circulation system 200 includes at least a portion of the product generated in the fuel cell system 100 in the fuel cell. And refeed to the reactants of system 100.
- the fuel cell system 100 may be configured as a system for producing electrical energy through chemical energy by reaction of a predetermined reactant. That is, the fuel cell system 100 is a system for producing electrical energy through chemical energy generated by oxidation of a reactant used as fuel, and a predetermined product may be generated as the reactants react.
- the product may for example be a predetermined gas.
- the term "product" herein refers to a state in which a part of the supplied reactant does not react as the reaction efficiency is not 100%, in addition to the material generated by completing the reaction as the reactants react in the fuel cell system 100.
- the concept includes a reactant to be discharged, and refers to all materials discharged from the fuel cell system 100.
- the fuel cell system 100 may include an anode pole 110, a cathode pole 120, and an electrolyte located between the anode pole 110 and the cathode pole 120.
- the fuel cell system 100 may be various systems such as phosphoric acid type, molten carbonate type, solid electrolyte type, and solid polymer type, depending on the type of electrolyte, but the fuel cell system 100 according to the present invention may be a molten carbonate type. Fuel cell system 100 may be used.
- the anode pole 110 functions as an anode to which a predetermined fuel is supplied among the reactants, and the fuel may be, for example, hydrogen.
- the cathode electrode 120 may function as an oxygen electrode supplied with oxygen and carbon dioxide in a reactant. Accordingly, the fuel cell system 100 according to the present invention may be configured as a pure oxygen combustion device using pure oxygen.
- Hydrogen may be injected from the anode pole 110 to generate electrons by an oxidation reaction, and oxygen and carbon dioxide may be supplied from the cathode pole 120 to generate carbonate ions.
- the carbonate ions may migrate from the cathode pole 120 to the anode pole 110 through an electrolyte located between the anode pole 110 and the cathode pole 120.
- carbonate ions and hydrogen provided from the cathode pole 120 may react to generate water and carbon dioxide.
- water includes a gaseous state such as water vapor in addition to the liquid state, and is not limited thereto.
- power may be produced as the electrons generated at the anode pole 110 are energized via an external circuit.
- the product passing through the fuel cell system 100 is water generated through the reaction between the reactant hydrogen, oxygen and carbon dioxide In addition to and carbon dioxide, it may contain hydrogen and oxygen that remain unreacted. That is, the product may include hydrogen, oxygen, water, carbon dioxide.
- the circulation system 200 is configured to circulate the product and to re-supply at least some of the product produced in the fuel cell system 100 to the reactants of the fuel cell system 100.
- At least some of the products produced in the fuel cell system 100 may be circulated to be reused as reactants in the fuel cell system 100.
- the circulation system 200 may separate carbon dioxide in the product and resupply the separated carbon dioxide to a reactant of the fuel cell system 100.
- the power generation system 1 includes a fuel cell system 100 and a circulation system 200, it is possible to reuse a product generated in the fuel cell system 100 as a reactant of the fuel cell system 100. Can be. Therefore, the power generation efficiency of the overall power generation system 1 is improved, and it is possible to prevent the discharge of products that may act as a cause of environmental pollution.
- the circulation system 200 recycles carbon dioxide in the product of the fuel cell system 100, it may contribute to suppressing the generation of pollutants by suppressing the emission of carbon dioxide, which is the cause of global warming.
- the circulation system 200 includes a separation device 210 for separating each component of the product produced in the fuel cell system 100, the circulation system 200 may be configured to resupply the separation separated through the separation device 210 to the reactants of the fuel cell system 100.
- the separation device 210 may be, for example, a phase separator 210, and the phase separation device 210 may separate each material included in the product.
- the separation device 210 may separate carbon dioxide and water vapor by using the boiling point difference between the carbon dioxide and water.
- the carbon dioxide and the water are separated by the separating device 210, and the circulation system 200 may supply the separated carbon dioxide to the cathode pole 120 of the fuel cell system 100.
- the separation device 210 further has a configuration capable of separating predetermined oxygen and hydrogen, and provides the separated oxygen and hydrogen to the anode pole 110 and the cathode pole 120, respectively.
- the power generation system 1 includes the circulation system 200 including the separation device 210, the recycling efficiency of the product generated in the fuel cell may be further increased. Meanwhile, as described above, carbon dioxide may be separated and reused, thereby contributing to the prevention of environmental pollution.
- the combustion system 300 further includes, and the combustion system 300 is configured to react with hydrogen and oxygen included in the product to generate carbon dioxide and water. .
- System 300 may be provided to generate carbon dioxide and water vapor from the oxygen and hydrogen.
- the combustion system 300 is installed at the rear of the fuel cell system 100 and may react with the unreacted oxygen and hydrogen to generate carbon dioxide and water vapor.
- the combustion system 300 may be composed of a catalytic combustion system 300 using a predetermined catalyst.
- the power generation system 1 further includes a turbine power generation system 400, wherein the turbine power generation system 400 is generated in the combustion system 300 The product rotates the turbine to produce power.
- the turbine power generation system 400 may be further provided to generate electricity using the thermal energy of the gas. Accordingly, the turbine power generation system 400 may be installed at the rear end of the combustion system 300, and may generate electrical energy by rotating the turbine through the hot gas.
- the power generation system 1 may include the fuel cell system 100 and the turbine power generation system 400, and thus may be configured as the hybrid power generation system 1. Accordingly, power generation through a fuel cell and power generation by a turbine using a high-temperature product generated from the fuel cell may be performed together, thereby further improving power output and energy utilization efficiency.
- the power generation system 1 of the present invention includes a heat exchange device 500 for recovering the heat energy of at least a portion of the product produced in the fuel cell system 100; It may further include.
- the heat exchange device 500 may be connected to the circulation system 200 to exchange heat and external heat of the product of the fuel cell system 100 circulated through the circulation system 200.
- the heat exchange device 500 may be provided at a rear end of the turbine power generation system 400, and may be provided to exchange heat and external heat of the gas passing through the turbine power generation system 400. That is, as the steam and carbon dioxide generated by the combustion of oxygen and hydrogen through the combustion system 300 is composed of a high temperature gas, it is used to produce power in the turbine power generation system 400, the turbine power generation system A predetermined heat exchange device 500 for exchanging heat and external heat may be provided to utilize the thermal energy remaining in the gas passing through the 400.
- the heat exchange device 500 may be configured to have a predetermined pipe structure, for example, so that the exchanged heat may be used for heating or the like.
- the overall energy utilization efficiency of the power generation system 1 according to the present invention can be further increased.
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Abstract
Description
Claims (9)
- 전력을 생산하는 발전 시스템에 있어서,상기 발전 시스템은,공급된 반응물을 반응시켜 전력을 생산하는 연료 전지 시스템; 및상기 연료 전지 시스템에서 생성된 생성물을 순환시키는 순환 시스템을 포함하며,상기 순환 시스템은,상기 연료 전지 시스템에서 생성된 생성물 중 적어도 일부를 상기 연료 전지 시스템의 반응물로 재 공급하는 것을 특징으로 하는 발전 시스템.
- 청구항 1에 있어서,상기 연료 전지 시스템은,반응물의 반응이 이루어지는 애노드 극, 및 캐소드 극을 포함하며,상기 애노드 극에는 수소가 공급되며,상기 캐소드 극에는 산소 및 이산화탄소가 공급되는 발전 시스템.
- 청구항 1에 있어서,상기 순환 시스템은,상기 연료 전지 시스템에서 생성된 생성물 중 적어도 일부를 분리하여 상기 연료 전지 시스템의 반응물로 재 공급하는 분리 장치를 포함하는 발전 시스템.
- 청구항 3에 있어서,상기 분리 장치는,상기 연료 전지 시스템에서 생성된 생성물 중 이산화탄소를 분리하여 상기 연료 전지 시스템에 재 공급하는 발전 시스템.
- 청구항 4에 있어서,상기 분리 장치는,비등점의 차이를 이용하는 상 분리 장치인 발전 시스템.
- 청구항 1에 있어서,연소 시스템을 더 포함하며,상기 연소 시스템은,상기 연료 전지 시스템 후단에 배치되며, 상기 생성물에 포함된 산소 및 수소를 반응시켜 물과 이산화탄소를 생성하는 발전 시스템.
- 청구항 6에 있어서,상기 연소 시스템은,소정의 촉매를 사용하는 촉매 연소 시스템인 발전 시스템.
- 청구항 6에 있어서,상기 발전 시스템은,터빈을 포함하며 상기 터빈의 회전으로 전력을 생산하는 터빈 발전 시스템을 더 포함하며,상기 터빈 발전 시스템은,상기 연소 시스템 후단에 배치되며, 상기 연소 시스템에서 생성된 물과 이산화탄소 중 적어도 하나를 사용하여 터빈을 회전시켜 전력을 생산하는 발전 시스템.
- 청구항 1에 있어서,상기 연소 시스템에서 생성된 생성물의 열과 외부의 열을 교환하는 열 교환 장치를 더 포함하는 발전 시스템.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
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US14/654,242 US20160197365A1 (en) | 2012-12-28 | 2013-08-14 | Power generation system |
JP2015551056A JP2016505197A (ja) | 2012-12-28 | 2013-08-14 | 発電システム |
CN201380068549.8A CN104885279A (zh) | 2012-12-28 | 2013-08-14 | 发电系统 |
EP13868662.1A EP2940770A4 (en) | 2012-12-28 | 2013-08-14 | ENERGY PRODUCTION SYSTEM |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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KR1020120155701A KR101397092B1 (ko) | 2012-12-28 | 2012-12-28 | 발전 시스템 |
KR10-2012-0155701 | 2012-12-28 |
Publications (1)
Publication Number | Publication Date |
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WO2014104526A1 true WO2014104526A1 (ko) | 2014-07-03 |
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PCT/KR2013/007329 WO2014104526A1 (ko) | 2012-12-28 | 2013-08-14 | 발전 시스템 |
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US (1) | US20160197365A1 (ko) |
EP (1) | EP2940770A4 (ko) |
JP (1) | JP2016505197A (ko) |
KR (1) | KR101397092B1 (ko) |
CN (1) | CN104885279A (ko) |
WO (1) | WO2014104526A1 (ko) |
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KR101954969B1 (ko) * | 2017-06-19 | 2019-03-07 | 삼성중공업 주식회사 | 기체 생산 설비 및 기체 생산 방법 |
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US4921765A (en) * | 1989-06-26 | 1990-05-01 | The United States Of America As Represented By The United States Department Of Energy | Combined goal gasifier and fuel cell system and method |
JP4357819B2 (ja) * | 2002-09-17 | 2009-11-04 | 株式会社Ihi | 燃料電池とマイクロガスタービンのコンバインド発電設備の熱電比変更方法 |
US7517372B2 (en) * | 2004-02-26 | 2009-04-14 | General Motors Corporation | Integrated fuel processor subsystem with quasi-autothermal reforming |
JP2008291081A (ja) * | 2007-05-23 | 2008-12-04 | Central Res Inst Of Electric Power Ind | ガス化設備 |
WO2010044113A1 (en) * | 2008-10-15 | 2010-04-22 | Ansaldo Fuel Cells S.P.A. | Apparatus and method for capturing carbon dioxide from combustion exhaust gas and generating electric energy by means of mcfc systems |
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2012
- 2012-12-28 KR KR1020120155701A patent/KR101397092B1/ko active IP Right Grant
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2013
- 2013-08-14 JP JP2015551056A patent/JP2016505197A/ja active Pending
- 2013-08-14 US US14/654,242 patent/US20160197365A1/en not_active Abandoned
- 2013-08-14 CN CN201380068549.8A patent/CN104885279A/zh active Pending
- 2013-08-14 EP EP13868662.1A patent/EP2940770A4/en not_active Withdrawn
- 2013-08-14 WO PCT/KR2013/007329 patent/WO2014104526A1/ko active Application Filing
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JPH06275291A (ja) * | 1993-03-23 | 1994-09-30 | Sanyo Electric Co Ltd | 溶融炭酸塩型燃料電池システム |
JPH1126004A (ja) * | 1997-07-02 | 1999-01-29 | Toshiba Corp | 発電システム |
KR20040038739A (ko) * | 2002-10-28 | 2004-05-08 | 휴렛-팩커드 디벨롭먼트 컴퍼니, 엘 피 | 열을 교환하는 촉매 연소기를 이용한 연료전지 |
KR20070043044A (ko) * | 2004-10-19 | 2007-04-24 | 자이단호징 덴료쿠추오켄큐쇼 | 복합 발전설비 |
JP2007311200A (ja) * | 2006-05-18 | 2007-11-29 | Nippon Telegr & Teleph Corp <Ntt> | 燃料電池システム |
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Also Published As
Publication number | Publication date |
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US20160197365A1 (en) | 2016-07-07 |
EP2940770A1 (en) | 2015-11-04 |
EP2940770A4 (en) | 2016-08-03 |
CN104885279A (zh) | 2015-09-02 |
JP2016505197A (ja) | 2016-02-18 |
KR101397092B1 (ko) | 2014-05-19 |
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