DK2474067T3 - Anordning til generering af en gas, der kan anvendes til opstart og lukning af en brændselscelle - Google Patents
Anordning til generering af en gas, der kan anvendes til opstart og lukning af en brændselscelle Download PDFInfo
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- DK2474067T3 DK2474067T3 DK10814572.3T DK10814572T DK2474067T3 DK 2474067 T3 DK2474067 T3 DK 2474067T3 DK 10814572 T DK10814572 T DK 10814572T DK 2474067 T3 DK2474067 T3 DK 2474067T3
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- Prior art keywords
- reducing gas
- fuel
- oxidant
- fuel cell
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- 239000000446 fuel Substances 0.000 title claims description 327
- 239000007789 gas Substances 0.000 claims description 345
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 201
- 239000007800 oxidant agent Substances 0.000 claims description 201
- 230000001590 oxidative effect Effects 0.000 claims description 189
- 239000000203 mixture Substances 0.000 claims description 151
- 229910052757 nitrogen Inorganic materials 0.000 claims description 102
- 230000003197 catalytic effect Effects 0.000 claims description 80
- 239000001301 oxygen Substances 0.000 claims description 73
- 229910052760 oxygen Inorganic materials 0.000 claims description 73
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 71
- 239000003054 catalyst Substances 0.000 claims description 67
- 239000004215 Carbon black (E152) Substances 0.000 claims description 34
- 229930195733 hydrocarbon Natural products 0.000 claims description 34
- 150000002430 hydrocarbons Chemical class 0.000 claims description 34
- 238000010438 heat treatment Methods 0.000 claims description 22
- 238000004891 communication Methods 0.000 claims description 19
- 239000012530 fluid Substances 0.000 claims description 19
- 238000006555 catalytic reaction Methods 0.000 claims description 16
- 239000003792 electrolyte Substances 0.000 claims description 15
- 230000009467 reduction Effects 0.000 claims description 13
- 239000012528 membrane Substances 0.000 claims description 12
- 238000002156 mixing Methods 0.000 claims description 12
- 238000000926 separation method Methods 0.000 claims description 11
- 238000011144 upstream manufacturing Methods 0.000 claims description 8
- 150000002829 nitrogen Chemical class 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- 239000011874 heated mixture Substances 0.000 claims description 2
- 244000309464 bull Species 0.000 claims 2
- 238000007599 discharging Methods 0.000 claims 2
- 239000003570 air Substances 0.000 description 123
- 238000010926 purge Methods 0.000 description 27
- 238000000034 method Methods 0.000 description 22
- 238000004519 manufacturing process Methods 0.000 description 20
- 230000008569 process Effects 0.000 description 16
- 230000015572 biosynthetic process Effects 0.000 description 14
- 229910002091 carbon monoxide Inorganic materials 0.000 description 14
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 13
- 238000006243 chemical reaction Methods 0.000 description 13
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 13
- -1 oxygen ions Chemical class 0.000 description 13
- 238000003786 synthesis reaction Methods 0.000 description 13
- 230000001276 controlling effect Effects 0.000 description 12
- 239000001257 hydrogen Substances 0.000 description 11
- 229910052739 hydrogen Inorganic materials 0.000 description 11
- 238000001514 detection method Methods 0.000 description 9
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 8
- 230000003647 oxidation Effects 0.000 description 8
- 238000007254 oxidation reaction Methods 0.000 description 8
- 239000000047 product Substances 0.000 description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 7
- 238000013459 approach Methods 0.000 description 7
- 230000006378 damage Effects 0.000 description 7
- 238000002485 combustion reaction Methods 0.000 description 6
- 238000003487 electrochemical reaction Methods 0.000 description 6
- 150000002431 hydrogen Chemical class 0.000 description 6
- 230000007704 transition Effects 0.000 description 6
- 238000001816 cooling Methods 0.000 description 5
- 230000003247 decreasing effect Effects 0.000 description 5
- 230000006870 function Effects 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 230000005012 migration Effects 0.000 description 5
- 238000013508 migration Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 239000006227 byproduct Substances 0.000 description 4
- 239000001569 carbon dioxide Substances 0.000 description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 239000003574 free electron Substances 0.000 description 4
- 239000003345 natural gas Substances 0.000 description 4
- 238000010248 power generation Methods 0.000 description 4
- 229910052717 sulfur Inorganic materials 0.000 description 4
- 239000011593 sulfur Substances 0.000 description 4
- 239000000470 constituent Substances 0.000 description 3
- 239000002826 coolant Substances 0.000 description 3
- 230000005611 electricity Effects 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000002594 sorbent Substances 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 239000012080 ambient air Substances 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 239000002360 explosive Substances 0.000 description 2
- 230000000977 initiatory effect Effects 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 2
- 230000004792 oxidative damage Effects 0.000 description 2
- 238000009428 plumbing Methods 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 230000004044 response Effects 0.000 description 2
- 229910000851 Alloy steel Inorganic materials 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 230000003466 anti-cipated effect Effects 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 238000007084 catalytic combustion reaction Methods 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000012809 cooling fluid Substances 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000011143 downstream manufacturing Methods 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000005304 joining Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 229920005594 polymer fiber Polymers 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 230000002459 sustained effect Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
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
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
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- H—ELECTRICITY
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- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04223—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
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- H01M8/04223—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
- H01M8/04225—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells during start-up
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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
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- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04223—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
- H01M8/04228—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells during shut-down
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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
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- H01M8/04223—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
- H01M8/04231—Purging of the reactants
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
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- H01M8/04223—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
- H01M8/04268—Heating of fuel cells during the start-up of the fuel cells
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- H—ELECTRICITY
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- 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
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/043—Processes for controlling fuel cells or fuel cell systems applied during specific periods
- H01M8/04303—Processes for controlling fuel cells or fuel cell systems applied during specific periods applied during shut-down
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- H—ELECTRICITY
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- H01M8/04313—Processes for controlling fuel cells or fuel cell systems characterised by the detection or assessment of variables; characterised by the detection or assessment of failure or abnormal function
- H01M8/0432—Temperature; Ambient temperature
- H01M8/04328—Temperature; Ambient temperature of anode reactants at the inlet or inside the fuel cell
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- H—ELECTRICITY
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- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
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- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
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- H01M8/04313—Processes for controlling fuel cells or fuel cell systems characterised by the detection or assessment of variables; characterised by the detection or assessment of failure or abnormal function
- H01M8/0438—Pressure; Ambient pressure; Flow
- H01M8/04425—Pressure; Ambient pressure; Flow at auxiliary devices, e.g. reformers, compressors, burners
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- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/04694—Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
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- H01M8/04731—Temperature of other components of a fuel cell or fuel cell stacks
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- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
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- H01M8/04701—Temperature
- H01M8/04738—Temperature of auxiliary devices, e.g. reformer, compressor, burner
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- H—ELECTRICITY
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- 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
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/04694—Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
- H01M8/04746—Pressure; Flow
- H01M8/04776—Pressure; Flow at auxiliary devices, e.g. reformer, compressor, burner
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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
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- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/04694—Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
- H01M8/04791—Concentration; Density
- H01M8/04798—Concentration; Density of fuel cell 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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/04694—Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
- H01M8/04955—Shut-off or shut-down of fuel cells
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- H—ELECTRICITY
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- 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
- H01M8/0687—Reactant purification by the use of membranes or filters
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- H—ELECTRICITY
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- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/241—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
- H01M8/2425—High-temperature cells with solid electrolytes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2256/00—Main component in the product gas stream after treatment
- B01D2256/10—Nitrogen
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/10—Single element gases other than halogens
- B01D2257/104—Oxygen
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- H—ELECTRICITY
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- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
- H01M2008/1293—Fuel cells with solid oxide electrolytes
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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
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Claims (4)
- -1 - ANORDNING TIL GENERERING AF EN GAS, DER KAN ANVENDES TIL OPSTART OG LUKNING AF EN BRÆNDSELSCELLE •ATENTKRAV Reduktionsgasgenerator (14) til opstart og lukning af en brændselscelle (12), hvilken generator mfatter: en oxideringsmiddelkilde, der er struktureret til at tilføre et oxideringsmiddel med et lavt oxygen- 02) indhold, hvilket oxideringsmiddel med lavt 02-indhold har et 02-indhold, der er mindre end indholdet i len atmosfæriske luft; en brændstofindgang (38), der er konfigureret til at modtage et carbonhybridbrændstof; et blandekammer (32), der står i fluidforbindelse med oxideringsmiddelkilden og i fluidforbindelse aed brændstofindgangen, hvilket blandekammer er struktureret til at modtage carbonhybridbrændstoffet og ixideringsmidlet med lavt 02-indhold og til at udlede en tilførselsblanding, der både indeholder arbonhybridbrændstoffet og oxideringsmidlet med lavt 02-indhold; en katalytisk reaktor (34), der står i fluidforbindelse med blandekammeret, hvilken katalytisk saktor er struktureret til at modtage tilførselsblandingen og til katalytisk at omdanne tilførselsblandingen til n reduktionsgas; og en reduktionsgasudgang, der fluidmæssigt er koblet til den katalytiske reaktor og står i luidforbindelse med mindst én af en anode (20) og en reformer (26) for brændselscellen, hvilken sduktionsgasudgang kan dirigere reduktionsgassen til den mindst én af brændselscellens anode og sformer, hvilken reduktionsgasgenerator endvidere indbefatter et styresystem (96), der er konfigureret til at ksekvere programinstruktioner for at regulere en styretemperatur ved at variere både 02-indholdet i ixideringsmidlet med lavt 02-indhold og forholdet mellem tilførselsblandingens oxideringsmiddel og irændstof. Reduktionsgasgenerator (14) ifølge krav 1, hvilken generator endvidere omfatter en itrogengenerator (54), der kan udlede oxygen (02) fra luft og udlede det resterende i form af en nitrogenrig ;as, hvilken nitrogenrig gas udgør mindst en del af oxideringsmidlet med lavt 02-indhold. Reduktionsgasgenerator (14) ifølge krav 2, hvilken generator endvidere omfatter et aftindføringssystem, der er koblet til nitrogengeneratorens udgang, hvilket luftindføringssystem er truktureret til variabelt at tilføre luft til den nitrogenrige gas for at variere 02-indholdet i oxideringsmidlet aed lavt 02-indhold. Reduktionsgasgenerator (14) ifølge krav 2, hvilken generator endvidere indbefatter en ventil, der er truktureret til at tilføre en styret mængde luft til en af den nitrogenrige gas og tilførselsblandingen. Reduktionsgasgenerator (14) ifølge krav 2, hvor nitrogengeneratoren indbefatter en itrogenseparationsmembran (56), der er konfigureret til at separere nitrogen fra luft. '. Reduktionsgasgenerator (14) ifølge krav 1, hvilken generator endvidere omfatter en tyretemperatursensor (84) og en 02-sensor (66), der forbindelsesmæssigt er koblet til styresystemet (96). Reduktionsgasgenerator (14) ifølge krav 1, hvilken generator endvidere omfatter: -2 - en oxideringsmiddelreguleringsventil (62), der forbindelsesmæssigt er koblet til styresystemet (96), ivilken oxideringsmiddelreguleringsventil er struktureret til at styre en strøm af oxideringsmidlet, der [irigeres ved hjælp af styresystemet; og en brændstofreguleringsventil (46), der forbindelsesmæssigt er koblet til styresystemet, hvilken irændstofrcgulcringsventil er struktureret til at styre en strøm af carbonhybridbrændstoffet, der dirigeres ed hjælp af styresystemet, hvor styresystemet er konfigureret til at eksekvere programinstruktioner for at variere forholdet nellem oxideringsmiddel og brændstof ved at styre udgangen fra mindst én af brændstofreguleringsventilen ig oxideringsmiddelreguleringsventilen. Reduktionsgasgenerator (14) ifølge krav 1, hvor styresystemet (96) er konfigureret til at eksekvere irograminstruktioner for selektivt at variere et indhold af brændbare stoffer i reduktionsgassen, mens der ipretholdes en udvalgt temperatur på reduktionsgassen ved både at variere oxideringsmidlets 02-indhold og brholdet mellem tilførselsblandingens oxideringsmiddel og brændstof. '. Reduktionsgasgenerator (14) ifølge krav 8, hvilken generator endvidere omfatter mindst to af en tyretemperatursensor (84), en oxygensensor (66) og en sensor (86) til detektering af brændbare stoffer i eduktionsgassen, hvilke sensorer er forbindelsesmæssigt koblet til styresystemet (96).0. Reduktionsgasgenerator (14) ifølge krav 1, hvilken generator endvidere omfatter en varmeveksler 88), der fluidmæssigt er tilkoblet på nedstrømssiden af den katalytiske reaktor (34), hvilken varmeveksler r konfigureret til at styre en temperatur på reduktionsgassen.1. Reduktionsgasgenerator (14) ifølge krav 1, hvilken generator endvidere omfatter en arme anordning (74) på opstrømssiden af den katalytiske reaktor (34), hvilken varmeanordning er onfigureret til at initiere en katalytisk reaktion ved den katalytiske reaktors katalysator (36) ved at opvarme aindst en del af tilførselsblandingen og tilføre den opvarmede blanding til den katalytiske reaktor.
- 2. Reduktionsgasgenerator (14) ifølge krav 11, hvor varmeanordningen (74) indbefatter et legeme 76), der er konfigureret til kontinuerligt at opretholde en temperatur ved én af ved og over en katalysator-36) driftstemperatur for tilførselsblandingen under normale anvendelser af brændselscellen (12).
- 3. Reduktionsgasgenerator (14) ifølge krav 1, hvilken generator endvidere omfatter mindst én af: en katalysatorvarmeanordning (80), der er konfigureret til at bevare den katalytiske reaktors (34) :atalysator (36) ved en temperatur på én af ved og over en katalysatordriftstemperatur for ilførselsblandingen under normale anvendelser af brændselscellen (12); og en anden varmeanordning (82), der er placeret stødende op til indgangen til den katalytiske reaktor 'g struktureret til at initiere katalytisk reaktion af tilførselsblandingen i en opstrømsdel af den katalytiske s aktor.
- 4. Brændselscellesystem (10), der omfatter: en brændselscelle (12), der indbefatter en anode (20), en katode (24), en elektrolyt (22), der er obiet til anoden og katoden, og en reformer (26); og en reduktionsgasgenerator (14), der er konfigureret til opstart og lukning af brændselscellen, ivilken reduktionsgasgenerator indbefatter: -3 - en oxideringsmiddelkilde, der er struktureret til at tilføre en oxideringsmiddelstrøm med lavt oxygen- (02) indhold, hvilken oxideringsmiddelstrøm med lavt 02-indhold har et 02-indhold, der er mindre end indholdet i den atmosfæriske luft; en brændstofindgang (38), der er konfigureret til at modtage et carbonhybridbrændstof; et blandekammer (32), der står i fluidforbindelse med oxideringsmiddelkilden og i fluidforbindelse med brændstofindgangen, hvilket blandekammer er struktureret til at modtage carbonhybridbrændstoffet og oxideringsmiddelstrømmen med lavt 02-indhold og til at udlede en tilførselsblanding, der indeholder både carbonhybridbrændstoffet og oxideringsmiddelstrømmen med lavt 02-indhold; en katalytisk reaktor (34), der står i fluidforbindelse med blandekammeret, hvilken katalytisk reaktor er struktureret til at modtage tilførselsblandingen og til katalytisk at omdanne tilførselsblandingen til en reduktionsgas; og en reduktionsgasudgang, der fluidmæssigt er koblet til den katalytiske reaktor og står i fluidforbindelse med mindst én af anoden og reformeren, hvilken reduktionsgasudgang kan dirigere reduktionsgassen til den mindst ene af anoden og reformeren, hvilken reduktionsgasgenerator endvidere indbefatter et styresystem (96), der er konfigureret til at eksekvere programinstruktioner for at regulere en styretemperatur ved at variere både 02-indholdet i oxideringsmidlet med lavt 02-indhold og forholdet mellem tilførselsblandingens oxideringsmiddel og brændstof.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US12/554,460 US8668752B2 (en) | 2009-09-04 | 2009-09-04 | Apparatus for generating a gas which may be used for startup and shutdown of a fuel cell |
| PCT/US2010/047850 WO2011029024A1 (en) | 2009-09-04 | 2010-09-03 | Apparatus for generating a gas which may be used for startup and shutdown of a fuel cell |
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| DK2474067T3 true DK2474067T3 (da) | 2016-11-21 |
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| Country | Link |
|---|---|
| US (1) | US8668752B2 (da) |
| EP (2) | EP2474067B1 (da) |
| KR (1) | KR101795082B1 (da) |
| AU (1) | AU2010289291B2 (da) |
| CA (2) | CA2773117C (da) |
| DK (1) | DK2474067T3 (da) |
| ES (1) | ES2588228T3 (da) |
| WO (1) | WO2011029024A1 (da) |
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-
2009
- 2009-09-04 US US12/554,460 patent/US8668752B2/en active Active
-
2010
- 2010-09-03 ES ES10814572.3T patent/ES2588228T3/es active Active
- 2010-09-03 CA CA2773117A patent/CA2773117C/en active Active
- 2010-09-03 KR KR1020127008147A patent/KR101795082B1/ko not_active Expired - Fee Related
- 2010-09-03 EP EP10814572.3A patent/EP2474067B1/en active Active
- 2010-09-03 AU AU2010289291A patent/AU2010289291B2/en not_active Ceased
- 2010-09-03 EP EP16176065.7A patent/EP3091597A3/en not_active Withdrawn
- 2010-09-03 WO PCT/US2010/047850 patent/WO2011029024A1/en not_active Ceased
- 2010-09-03 CA CA2901032A patent/CA2901032A1/en not_active Abandoned
- 2010-09-03 DK DK10814572.3T patent/DK2474067T3/da active
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| Publication number | Publication date |
|---|---|
| WO2011029024A1 (en) | 2011-03-10 |
| US20110059377A1 (en) | 2011-03-10 |
| CA2773117A1 (en) | 2011-03-10 |
| AU2010289291A1 (en) | 2012-03-29 |
| AU2010289291B2 (en) | 2015-05-28 |
| KR20120049382A (ko) | 2012-05-16 |
| EP3091597A2 (en) | 2016-11-09 |
| ES2588228T3 (es) | 2016-10-31 |
| CA2773117C (en) | 2015-11-24 |
| EP2474067A4 (en) | 2014-01-08 |
| US8668752B2 (en) | 2014-03-11 |
| CA2901032A1 (en) | 2011-03-10 |
| KR101795082B1 (ko) | 2017-11-07 |
| EP2474067A1 (en) | 2012-07-11 |
| EP3091597A3 (en) | 2017-01-18 |
| EP2474067B1 (en) | 2016-07-27 |
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