JPS5691375A - Fuel battery - Google Patents

Fuel battery

Info

Publication number
JPS5691375A
JPS5691375A JP16808779A JP16808779A JPS5691375A JP S5691375 A JPS5691375 A JP S5691375A JP 16808779 A JP16808779 A JP 16808779A JP 16808779 A JP16808779 A JP 16808779A JP S5691375 A JPS5691375 A JP S5691375A
Authority
JP
Japan
Prior art keywords
reactor
modification
reaction
fuel battery
heated
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP16808779A
Other languages
Japanese (ja)
Inventor
Ko Watanabe
Hisashi Morimoto
Kengo Uematsu
Hiroyuki Kako
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP16808779A priority Critical patent/JPS5691375A/en
Publication of JPS5691375A publication Critical patent/JPS5691375A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • H01M8/0625—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 in a modular combined reactor/fuel cell structure
    • 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

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Fuel Cell (AREA)

Abstract

PURPOSE:To increase thermal efficiency and to make the size smaller by inserting a modification reactor in a fuel battery system and utilizing reaction heat generated by a discharge reaction for a source for heating the modification reactor. CONSTITUTION:A mixture gas 8 of hydrocarbon and steam fed in a modification reactor 5 is heated to a definite temperature with a burner 6 in a heating chamber 7, before a fuel battery 1 is discharged, whereby modification reaction is carried out in the presence of a catalyst. The modified gas 9 including H2, CO, CO2, methane and so on is taken out of the reactor 5 and fed to a cathode 3. When discharging is started, the temperature of the battery body 1 is raised to, for example, 700-800 deg.C, and the reactor 5 is heated by the reaction heat. Therefore, modification reaction is carried out all over the reactor while the battery body 1 is cooled due to feeding heat to the reactor 5, and discharge reaction is accelerated thereby.
JP16808779A 1979-12-26 1979-12-26 Fuel battery Pending JPS5691375A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16808779A JPS5691375A (en) 1979-12-26 1979-12-26 Fuel battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16808779A JPS5691375A (en) 1979-12-26 1979-12-26 Fuel battery

Publications (1)

Publication Number Publication Date
JPS5691375A true JPS5691375A (en) 1981-07-24

Family

ID=15861596

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16808779A Pending JPS5691375A (en) 1979-12-26 1979-12-26 Fuel battery

Country Status (1)

Country Link
JP (1) JPS5691375A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1991011034A1 (en) * 1990-01-10 1991-07-25 International Fuel Cells Corporation Molten carbonate fuel cell power plant

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1991011034A1 (en) * 1990-01-10 1991-07-25 International Fuel Cells Corporation Molten carbonate fuel cell power plant

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