DK2474065T3 - Fremgangsmåde til generering af en gas, der kan anvendes til opstart og nedlukning af en brændselscelle - Google Patents

Fremgangsmåde til generering af en gas, der kan anvendes til opstart og nedlukning af en brændselscelle Download PDF

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DK2474065T3
DK2474065T3 DK10814564.0T DK10814564T DK2474065T3 DK 2474065 T3 DK2474065 T3 DK 2474065T3 DK 10814564 T DK10814564 T DK 10814564T DK 2474065 T3 DK2474065 T3 DK 2474065T3
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reducing gas
fuel cell
feed mixture
fuel
content
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Mark Vincent Scotto
Daniel P Birmingham
Crispin L Debellis
Mark Anthony Perna
Gregory C Rush
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Lg Fuel Cell Systems Inc
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
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    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
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    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/384Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts the catalyst being continuously externally heated
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    • C01B13/00Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/02Preparation of oxygen
    • C01B13/0229Purification or separation processes
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    • C01B13/0251Physical processing only by making use of membranes
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    • C01B21/00Nitrogen; Compounds thereof
    • C01B21/04Purification or separation of nitrogen
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    • C01B21/0433Physical processing only
    • C01B21/0438Physical processing only by making use of membranes
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    • H01M8/04223Auxiliary 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
    • H01M8/04225Auxiliary 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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    • H01M8/04223Auxiliary 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
    • H01M8/04228Auxiliary 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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    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/043Processes for controlling fuel cells or fuel cell systems applied during specific periods
    • H01M8/04302Processes for controlling fuel cells or fuel cell systems applied during specific periods applied during start-up
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    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04694Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
    • H01M8/04701Temperature
    • H01M8/04708Temperature of fuel cell reactants
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    • H01M8/04694Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
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    • H01M8/2425High-temperature cells with solid electrolytes
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    • C01B2203/02Processes for making hydrogen or synthesis gas
    • C01B2203/0205Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0227Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
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    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/12Feeding the process for making hydrogen or synthesis gas
    • C01B2203/1205Composition of the feed
    • C01B2203/1211Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
    • C01B2203/1235Hydrocarbons
    • C01B2203/1241Natural gas or methane
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    • H01M8/04223Auxiliary 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
    • H01M8/04231Purging of the reactants
    • 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
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    • Y02E60/50Fuel cells

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  • Combustion & Propulsion (AREA)
  • Fuel Cell (AREA)
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Claims (8)

  1. DK/EP 2474065 T3 -1- FREMGANGSMÅDE TIL GENERERING AF EN GAS, DER KAN ANVENDES TIL OPSTART OG NEDLUKNING AFEN BRÆNDSELSCELLE VTENTKRAV Fremgangsmåde til opstart og nedlukning af en brændselscelle (12) ved anvendelse af en iuktionsgasgenerator (14), hvilken fremgangsmåde omfatter: modtagelse af luft i et luftindtag (48) til en reduktionsgasgenerator; generering af en strøm af oxideringsmiddel med lavt oxygen- (02) indhold med et oxygenindhold, r er mindre end indholdet i atmosfærisk luft under samme tryk- og temperaturforhold, ved anvendelse af indst delvist luft modtaget fra luftindtaget; initiering af strømning af en strøm af carbonhydridbrændsel i reduktionsgasgeneratoren; kombinering strømmen af carbonhydridbrændsel med strømmen af oxideringsmiddel med lavt 02-ihold for at opnå en tilførselsblanding; dirigering af tilførselsblandingen til en katalysator (36); katalytisk omdannelse af tilførselsblandingen til en reduktionsgas; dirigering af reduktionsgassen til mindst én af en anode (20) og en reformeringsanordning (26) for ændselscellen; og initiering af én af: en overgang af brændselscellen til en strømproduktionsfunktion og en overgang af brændselscellen fra strømproduktionsfunktionen. Fremgangsmåde ifølge krav 1, hvor overgangen af brændselscellen (12) til ømproduktionsfunktionen indbefatter tilførsel af strømme af et primært brændsel og et primært ideringsmiddel til brændselscellen; og hvor overgangen af brændselscellen fra ømproduktionsfunktionen indbefatter afbrydelse af strømmene af det primære brændsel og det primære ideringsmiddel til brændselscellen. Fremgangsmåde ifølge krav 1, hvilken fremgangsmåde endvidere omfatter generering af en xogenrig strøm fra luften modtaget fra luftindtaget (48), hvor den nitrogenrige strøm danner mindst en del strømmen af oxideringsmiddel med lavt oxygen- (02) indhold. Fremgangsmåde ifølge krav 1, hvilken fremgangsmåde endvidere omfatter opretholdelse af en lgt styretemperatur ved uafhængigt at variere både 02-indholdet i strømmen af oxideringsmiddel og rholdet mellem oxideringsmiddel/brændstof i tilførselsblandingen. Fremgangsmåde ifølge krav 4, hvilken fremgangsmåde endvidere omfatter styring af den valgte /retemperatur baseret på et detekteret 02-indhold i mindst én af strømmen af oxideringsmiddel og førselsblandingen. Fremgangsmåde ifølge krav 4, hvilken fremgangsmåde endvidere omfatter styring af en ømningshastighed for tilførselsblandingen under opretholdelse af den valgte styretemperatur ved at riere både 02-indholdet af strømmen af oxideringsmiddel og forholdet mellem ideringsmiddel/brændstof i tilførselsblandingen. DK/EP 2474065 T3 -2-
  2. 7. Fremgangsmåde ifølge krav 4, hvilken fremgangsmåde endvidere omfatter selektiv variation af reduktionsgassens indhold af brændbare stoffer.
  3. 8. Fremgangsmåde ifølge krav 7, hvilken fremgangsmåde endvidere omfatter selektiv variation af reduktionsgassens indhold af brændbare stoffer, mens den valgte styretemperatur opretholdes baseret på et 5 detekteret 02-indhold i mindst ét/én af oxideringsmidlet og tilførselsblandingen.
  4. 9. Fremgangsmåde ifølge krav 7, hvilken fremgangsmåde endvidere omfatter styring af en strømningshastighed for tilførselsblandingen, mens den selektive variation af reduktionsgassens indhold af brændbare stoffer foretages, mens den valgte styretemperatur opretholdes.
  5. 10. Fremgangsmåde ifølge krav 1, hvor reduktionsgassen fra starten produceres som en sikker gas, der 10 dirigeres til brændselscellen (12) under brændselscellens overgang til strømproduktionsfunktionen, hvilken fremgangsmåde endvidere omfatter en forøgelse af reduktionsgassens reduktionsstyrke ved at øge reduktionsgassens indhold af brændbare stoffer.
  6. 11. Fremgangsmåde ifølge krav 1, hvilken fremgangsmåde endvidere omfatter: generering af en nitrogenrig strøm fra luften modtaget fra luftindtaget (48); og 15 dirigering af mindst noget af den nitrogenrige strøm for at rense en komponent, der er forbundet med en brændselscelle (12).
  7. 12. Fremgangsmåde til nedlukning af en brændselscelle (12), hvilken fremgangsmåde omfatter: modtagelse en kommando om nedlukning af brændselscellen fra strømproduktionsfunktionen; modtagelse af luft fra et luftindtag (48); 20 generering af en nitrogenrig gasstrøm ved at ekstrahere oxygen (02) fra luften modtaget fra luftindtaget; initiering af en strøm af en strøm af carbonhydridbrændsel som reaktion på kommandoen; kombinering af strømmen af carbonhydridbrændsel med den nitrogenrige gasstrøm for at opnå en tilførselsblanding; 25 dirigering af tilførselsblandingen til mindst én af en opvarmer (74), en katalysator (36) og en indgang til katalysatoren, hvor den mindst ene af opvarmeren, katalysatoren og indgangen til katalysatoren er opvarmet til en foropvarmningstemperatur valgt til katalytisk selvantændelse af tilførselsblandingen; omdannelse af tilførselsblandingen til en reduktionsgas ved anvendelse af katalysatoren; og dirigering af reduktionsgassen til mindst én af en anode (20) og en reformeringsanordning (26) for 30 brændselscellen.
  8. 13. Fremgangsmåde ifølge krav 12, hvilken fremgangsmåde endvidere omfatter opretholdelse af den mindst ene af opvarmeren, katalysatoren og indgangen til katalysatoren ved den foropvarmningstemperatur, der er valgt til katalytisk selvantændelse af tilførselsblandingen under brændselscelledrift i strømproduktionsfunktion forud for modtagelse af kommandoen om nedlukning af brændselscellen.
DK10814564.0T 2009-09-04 2010-09-03 Fremgangsmåde til generering af en gas, der kan anvendes til opstart og nedlukning af en brændselscelle DK2474065T3 (da)

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US12/554,039 US8597841B2 (en) 2009-09-04 2009-09-04 Method for generating a gas which may be used for startup and shutdown of a fuel cell
PCT/US2010/047831 WO2011029014A1 (en) 2009-09-04 2010-09-03 Method for generating a gas which may be used for startup and shutdown of a fuel cell

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US (2) US8597841B2 (da)
EP (2) EP2930775B1 (da)
KR (2) KR101906090B1 (da)
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