US20050074644A1 - Fuel cell system - Google Patents

Fuel cell system Download PDF

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Publication number
US20050074644A1
US20050074644A1 US10/955,516 US95551604A US2005074644A1 US 20050074644 A1 US20050074644 A1 US 20050074644A1 US 95551604 A US95551604 A US 95551604A US 2005074644 A1 US2005074644 A1 US 2005074644A1
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United States
Prior art keywords
combustible gas
fuel cell
cell system
hydrogen
gas
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Abandoned
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US10/955,516
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English (en)
Inventor
Tetsuya Ueda
Shinji Miyauchi
Akinari Nakamura
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Panasonic Corp
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Matsushita Electric Industrial Co Ltd
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Assigned to MATSUSHITA ELECTRIC INDUSTRIAL CO., LTD. reassignment MATSUSHITA ELECTRIC INDUSTRIAL CO., LTD. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: MIYAUCHI, SHINJI, NAKAMURA, AKINARI, UEDA, TETSUYA
Publication of US20050074644A1 publication Critical patent/US20050074644A1/en
Assigned to PANASONIC CORPORATION reassignment PANASONIC CORPORATION CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: MATSUSHITA ELECTRIC INDUSTRIAL CO., LTD.
Priority to US12/489,549 priority Critical patent/US7736815B2/en
Abandoned legal-status Critical Current

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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
    • 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
    • H01M8/04313—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
    • H01M8/0444—Concentration; Density
    • 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
    • H01M8/04313—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
    • H01M8/04664—Failure or abnormal function
    • H01M8/04679—Failure or abnormal function of fuel cell stacks
    • 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
    • H01M8/04313—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
    • H01M8/04664—Failure or abnormal function
    • H01M8/04686—Failure or abnormal function of auxiliary devices, e.g. batteries, capacitors
    • 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
    • H01M8/04746—Pressure; Flow
    • H01M8/04753—Pressure; Flow of fuel cell reactants
    • 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
    • H01M8/04746—Pressure; Flow
    • H01M8/04776—Pressure; Flow at auxiliary devices, e.g. reformer, compressor, burner
    • 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
    • H01M8/0618—Reforming processes, e.g. autothermal, partial oxidation or steam reforming
    • 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
    • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2465—Details of groupings of fuel cells
    • H01M8/247—Arrangements for tightening a stack, for accommodation of a stack in a tank or for assembling different tanks
    • H01M8/2475—Enclosures, casings or containers of fuel cell stacks
    • 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
    • H01M8/04201—Reactant storage and supply, e.g. means for feeding, pipes
    • 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
    • H01M8/04223—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
    • 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 fuel cell system employed in, for example, stationary power generation apparatuses, or power supplies for automobile.
  • FIG. 9 is a view schematically showing an example of a construction of the conventional fuel cell system.
  • a conventional fuel cell system 600 comprises, within a package 51 , a fuel supply device 52 , a fuel cell 53 , and a DC/AC (direct current-to-alternate current) converter 54 .
  • the fuel supply device 52 is configured to supply a hydrogen-rich gas containing plentiful hydrogen (hereinafter referred to as hydrogen-rich gas) to the fuel cell 53 .
  • the fuel cell 53 is configured to carry out power generation to output a DC (direct current) of a predetermined voltage, using the hydrogen-rich gas supplied from the fuel supply device 52 .
  • the DC/AC converter 54 is configured to convert the DC of the predetermined voltage which is output from the fuel cell 53 into an AC of the predetermined voltage, and to output the AC.
  • the package 51 is provided with an inlet 56 to which a fan 55 is attached, and an air outlet 58 to which a combustible gas detector 57 which detects a combustible gas is attached (see Japanese Laid-Open Patent Application Publication No. Hei 03-254070, FIG. 1 ).
  • the fuel supply device 52 When the fuel cell system 600 is operated to generate an electric power, the fuel supply device 52 first generates the hydrogen-rich gas, and then supplies the hydrogen-rich gas to the fuel cell 53 through a predetermined pipe.
  • the fuel cell 53 generates an electric power using the hydrogen-rich gas supplied from the fuel supply device 52 .
  • the DC of the predetermined voltage generated in the fuel cell 53 is input to the DC/AC converter 54 .
  • the DC/AC converter 54 converts the DC of the predetermined voltage input from the fuel cell 53 into the AC of the predetermined voltage. Thereby, the AC of the predetermined voltage is output from the fuel cell system 600 .
  • ambient air is suctioned from the inlet 56 into the package 51 by using the fan 55 , and the air in the interior of the package 51 is exhausted from the air outlet 58 to outside of the package 51 through the combustible gas detector 57 .
  • the combustible gas detector 57 is capable of accurately detecting the leakage of the combustible gas so long as the combustible gas detector 57 is functioning properly. In other words, safety of the fuel cell system 600 can be ensured so long as the combustible gas detector 57 is functioning properly.
  • the detection capability of the combustible gas detector 57 degrades, for example, after an elapse of time, and hence detection sensitivity of the combustible gas detector 57 to the combustible gas degrades, the leakage of the combustible gas cannot be detected accurately. In such a case, safety of the fuel cell system 600 cannot be ensured.
  • the combustible gas detector 57 is incapable of detecting even the leakage of the combustible gas with a concentration which exceeds an upper limit of an allowable range. In this case, since safety measures cannot be taken for the fuel cell system 600 , it may be highly probable that the fuel system 600 malfunctions, for example.
  • the safety of the fuel cell system 600 may be ensured by inspecting the combustible gas detector 57 on a regular basis or by forcibly replacing the combustible gas detector 57 , assuming that the above-mentioned condition would take place. In that case, however, maintenance such as inspection and replacement of the combustible gas detector 57 must be carried out, irrespective of whether or not the combustible gas detector 57 is functioning properly. This may lead to increased cost in maintenance of the fuel cell system 600 .
  • the present invention has been developed under the circumstances, and an object of the present invention is to provide a fuel cell system capable of ensuring safety associated with leakage of a combustible gas and of reducing a maintenance cost.
  • a fuel cell system comprising, within a package, a fuel cell stack; a hydrogen-rich gas supply means configured to supply a hydrogen-rich gas; a combustible gas detector configured to detect leakage of a combustible gas which is the hydrogen-rich gas or a raw fuel gas which is a raw material of the hydrogen-rich gas within the package; a combustible gas guide pipe through which the combustible gas is guided into the package; and a controller; wherein the controller is configured to inject the combustible gas intermittently through the combustible gas guide pipe, and to perform a self-diagnostic process as to whether or not the combustible gas detector is functioning properly.
  • the fuel cell system is configured to self-diagnose the function of the combustible gas detector based on the gas actually used in the fuel cell system, malfunction or the like of the combustible gas detector can be reliably avoided.
  • the combustible gas guide pipe may be configured to branch from a combustible gas passage and to have an end positioned in the vicinity of the combustible gas detector, and the controller may be configured to inject the combustible gas intermittently toward the combustible gas detector through the combustible gas guide pipe, and to perform a self-diagnostic process as to whether or not the combustible gas detector is functioning properly.
  • the controller may be configured to inject the combustible gas intermittently toward the combustible gas detector through the combustible gas guide pipe, and to perform a self-diagnostic process as to whether or not the combustible gas detector is functioning properly.
  • the hydrogen-rich gas supply means may be a reformer configured to generate the hydrogen-rich gas from the raw fuel gas.
  • a reformer configured to generate the hydrogen-rich gas from the raw fuel gas.
  • the combustible gas guide pipe may be configured to branch from a position in a raw fuel gas supply passage connected to an inlet of the reformer. In such a construction, the raw fuel gas can be guided into the combustible gas guide pipe.
  • the combustible gas guide pipe may be configured to branch from a position in a hydrogen supply passage extending between the reformer and an anode of the fuel cell stack, and the raw fuel gas is used under a stopped state of the reformer and the hydrogen-rich gas is used during an operation of the reformer as a gas injected toward the combustible gas detector.
  • the kind of the gas injected toward the combustible gas detector can be selected according to an operating state of the fuel cell system.
  • the combustible gas guide pipe may be configured to branch from a position in an exhausted hydrogen passage connected to an anode of the fuel cell stack, and the raw fuel gas filled within the fuel cell stack to purge the hydrogen-rich gas when an operation of the fuel cell stack terminates is used as a gas injected toward the combustible gas detector.
  • the controller may be configured to close a raw fuel gas valve provided in a raw fuel gas supply passage when said combustible gas detector continues to detect the combustible gas after an elapse of predetermined time after the controller terminates injection of the combustible gas. By doing so, it is possible to inhibit the combustible gas from continuing to flow irrespective of the failure of the valve configured to be opened and closed to control the flow of the combustible gas.
  • An exhaust fan may be provided in the package in the vicinity of the combustible gas detector, and configured to dilute the injected combustible gas with ambient air and to exhaust the diluted combustible gas to outside of the package. Since the combustible gas injected toward the combustible gas detector is sufficiently diluted with air and then exhausted to outside the package, the combustible gas can be exhausted safely.
  • the controller may be configured to operate the exhaust fan intermittently during a stopped state of the fuel cell system to allow leakage of the combustible gas to be monitored during the stopped state of the fuel cell system. Since the leakage of the combustible gas can be also monitored under the stopped state of the operation of the fuel cell system, the safety of the fuel cell system can be ensured.
  • the controller may be configured to perform the self-diagnostic process in such a manner that the controller determines that life of the combustion gas detector has expired when detection sensitivity of the combustible gas detector to the injected combustible gas varies from an initial value and becomes outside an allowable range, and prohibits an operation of the fuel cell system. Since the operation of the fuel cell system is prohibited when the life of the combustible gas detector gas has expired, the safety of the fuel cell system can be ensured.
  • the controller may further cause a warning to be displayed when determining that the life of the combustible gas detector has expired. Thereby, since the warning is displayed when the life of the combustible gas detector has expired, the safety of the fuel cell system can be ensured.
  • the controller may be configured to set an injection interval of the combustible gas longer when a variation in the detection sensitivity of the combustible gas detector from an initial value is smaller than a predetermined value, and to set the injection interval shorter when the variation is larger than the predetermined value. Since the self-diagnostic process is carried out depending on the state of the combustible gas detector, degradation of the function of the combustible gas detector can be accurately recognized.
  • the controller may be configured to predict the life of the combustible gas detector from the self-diagnostic process, and to communicate information regarding the predicted life to a maintenance operator. By doing so, since the life of the combustible gas detector can be predicted in advance, a cost associated with maintenance can be reduced.
  • FIG. 1 is a view schematically showing a construction of a fuel cell system according to a first embodiment of the present invention
  • FIG. 2 is a flowchart showing self-diagnostic steps for a combustible gas detector according to the first embodiment of the present invention
  • FIG. 3 is a view schematically showing a construction of a fuel cell system according to a second embodiment of the present invention.
  • FIG. 4 is a flowchart showing self-diagnostic steps for a combustible gas detector according to the second embodiment of the present invention.
  • FIG. 5 is a view schematically showing a construction of a fuel cell system according to a third embodiment of the present invention.
  • FIG. 6 is a flowchart showing self-diagnostic steps for a combustible gas detector according to the third embodiment of the present invention.
  • FIG. 7 is a view schematically showing a construction of a fuel cell system according to a fourth embodiment of the present invention.
  • FIG. 8 is a view schematically showing another construction of the fuel cell system according to the fourth embodiment of the present invention.
  • FIG. 9 is a view schematically showing an example of a construction of the conventional fuel cell system.
  • FIG. 1 is view schematically showing a construction of a fuel cell system according to a first embodiment of the present invention.
  • the fuel cell system 100 comprises, within a package 18 provided with an inlet 19 and an outlet 20 , a reformer 1 equipped with a burner 2 and configured to generate a hydrogen-rich gas, i.e., function as a hydrogen-rich gas supply means, a fuel cell stack 7 including an anode 8 and a cathode 9 and configured to generate an electric power using the hydrogen-rich gas and air, three-way valves 15 and 16 configured to change passages of the hydrogen-rich gas or the like, valves 25 a and 27 a configured to open and close passages of a raw fuel gas or the like, a raw fuel gas valve 26 configured to open and close a passage of the raw fuel gas, a branch portion 24 a at which the passage of the raw fuel gas branches, a combustible gas detector 22 configured to detect a combustible gas, an exhaust fan 21 configured to ventilate the interior of the fuel cell system 100 , an air blower 13 configured to supply the air to the fuel cell stack 7 , and
  • a raw fuel gas supply passage 4 which is a combustible gas flow passage, is connected to an inlet 3 of the reformer 1 .
  • the raw fuel gas valve 26 , the branch portion 24 a , and the valve 27 a are provided at predetermined positions of the raw fuel gas supply passage 4 .
  • a combustible gas guide pipe 23 extends from the branch portion 24 a , and the valve 25 a is provided at a predetermined position of the combustible gas guide pipe 23 .
  • a tip end of the combustible gas guide pipe 23 is positioned in the vicinity of the combustible gas detector 22 .
  • the exhaust fan 21 is positioned adjacently to the combustible gas detector 22 .
  • the exhaust fan 21 is configured to suction the air within the package 18 and to exhaust the air from the outlet 20 . It will be appreciated that the tip end of the combustible gas guide pipe 23 may be located at any position within the package 18 other than the vicinity of the combustible gas detector 22 , which enables a self-diagnostic function described later to be performed.
  • a hydrogen-rich gas supply passage 6 is connected to an outlet 5 of the reformer 1 .
  • An end of the hydrogen-rich gas supply passage 6 is connected to the anode 8 of the fuel cell stack 7 .
  • An exhausted hydrogen passage 10 extends from the anode 8 , and an end of the exhausted hydrogen passage 10 is connected to the burner 2 equipped in the reformer 1 .
  • the three-way valves 15 and 16 are provided at predetermined positions of the hydrogen-rich gas supply passage 6 and the exhausted hydrogen passage 10 , respectively.
  • the three-way valve 15 is connected to the three-way valve 16 through a bypass 14 .
  • an air supply passage 11 extends from the air blower 13 , and an end of the air supply passage 11 is connected to the cathode 9 of the fuel cell stack 7 .
  • An exhausted air passage 12 extends from the cathode 9 to outside of the package 18 .
  • the controller 17 and above the components of the fuel cell system 100 are interconnected through predetermined wires 28 (entire of which are not illustrated in FIG. 1 ). And, the controller 17 is configured to properly control the components of the fuel cell system 100 by using the predetermined wires 28 . Thereby, the fuel cell system 100 operates.
  • the raw fuel gas for example, methane flows within the raw fuel gas supply passage 4 and into the reformer 1 through the inlet 3 .
  • the raw fuel gas within the reformer 1 is heated by the burner 2 .
  • the raw fuel gas is converted into the hydrogen-rich gas through a predetermined reforming reaction.
  • the hydrogen-rich gas containing plentiful hydrogen (hydrogen-rich gas) is supplied to the anode 8 of the fuel cell stack 7 through the hydrogen-rich gas supply passage 6 .
  • the air from the air blower 13 is supplied to the cathode 9 of the fuel cell stack 7 through the air supply passage 11 .
  • a chemical reaction between hydrogen contained in the hydrogen-rich gas and oxygen contained in air is conducted using the hydrogen-rich gas and the air.
  • a DC of a predetermined voltage is output from the fuel cell stack 7 .
  • Excess air, remaining unconsumed after the chemical reaction is exhausted from the fuel cell stack 7 to outside of the package 18 through the exhausted air passage 12 connected to the cathode 9 .
  • excess hydrogen-rich gas, remaining unconsumed after the chemical reaction is supplied to the burner 2 through the exhausted hydrogen passage 10 connected to the anode 8 .
  • the hydrogen-rich gas supplied through the exhausted hydrogen passage 10 is used as a heating fuel of the reforming reaction for generating the hydrogen-rich gas.
  • the three-way valves 15 and 16 are operated to allow the hydrogen-rich gas supply passage 6 to be connected to the exhausted hydrogen passage 10 through the bypass 14 so that the hydrogen-rich gas containing low-content hydrogen is supplied to the burner 2 rather than the fuel cell stack 7 . Also, within the package 18 , air flow is caused to occur in a way that ambient air is suctioned from the inlet 19 and exhausted from the outlet 20 by using the exhaust fan 21 .
  • the controller 17 closes the raw fuel gas valve 26 to cause the fuel cell system 100 to stop operation. Further, the controller 17 causes a warning to be displayed and so on as desired so that information indicating abnormality may be presented to a user of the fuel cell system 100 .
  • FIG. 2 is a flowchart showing self-diagnostic steps for the combustible gas detector 22 of the first embodiment of the present invention.
  • the controller 17 closes the valve 27 a (Step S 1 ) and opens the raw fuel gas valve 26 and the valve 25 a (Step S 2 ), under a stopped state of power generation, for example. Under this condition, the controller 17 injects the raw fuel gas, which is a combustible gas, for example, methane, from the tip end of the combustible gas guide pipe 23 toward the combustible gas detector 22 in a little amount and continuously (Step S 3 ).
  • the raw fuel gas which is a combustible gas, for example, methane
  • the controller 17 determines that the combustible gas detector 22 is functioning properly, and terminates the self-diagnostic process (YES in Step S 4 ).
  • the controller 17 recognizes that the combustible gas detector 22 is not functioning properly.
  • the controller 17 determines that the life of the combustible gas detector 22 has expired, and takes appropriate safety measures for ensuring safety of the fuel cell system 100 , for example, by displaying information regarding prohibition of the operation of the fuel cell system 100 , a warning, etc (Step S 5 ).
  • the series of self-diagnostic process in the fuel cell system 100 may be carried out during a power generation operation, as well as during the stopped state of the power generation operation.
  • the controller 17 opens the valve 25 a , the raw fuel gas valve 26 , and the valve 27 a in Step S 2 .
  • the raw fuel gas is supplied to the reformer 1 and the hydrogen-rich gas generated in the reformer 1 is supplied to the fuel cell stack 7 .
  • the fuel cell stack 7 carries out power generation to output the DC of the predetermined voltage.
  • Step S 4 when the controller 17 recognizes that the output voltage of the combustible gas detector 22 becomes not higher than the voltage corresponding to the combustible gas concentration within the predetermined range (NO in Step S 4 ), the controller 17 takes appropriate measures for ensuring safety of the fuel cell system 100 by displaying a warning, etc, and by closing the valve 26 (Step S 5 ).
  • the safety of the fuel cell system 100 can be satisfactorily ensured without continuously carrying out the self-diagnostic process (i.e., injection of the combustible gas toward the combustible gas detector 22 in Step S 3 ).
  • the safety of the fuel cell system 100 can be ensured by carrying out the self-diagnostic process intermittently, for example, once every other day or every several days.
  • the controller 17 determines that the life of the combustible gas detector 22 will expire soon, and decreases a time interval at which the combustible gas is injected toward the combustible gas detector 22 , thus effectively ensuring the safety of the fuel cell system 100 .
  • the combustible gas such as methane is injected within the package 18 although the amount is small (Step S 3 ). So, it is necessary to exhaust the combustible gas to outside of the package 18 after diluting the injected combustible gas by mixing with ambient air by using the exhaust fan 21 so that the concentration of the combustible gas becomes not higher than a lower limit at which explosion may take place. By doing so, the safety of the fuel cell system 100 can be ensured.
  • controller 17 may operate the exhaust fan 21 intermittently during the stopped state of power generation operation to monitor the leakage of the combustible gas all the time. This is very effective in ensuring the safety of the fuel cell system 100 .
  • the controller 17 may communicate the information regarding the combustible gas concentration, output from the combustible gas detector 22 , to a maintenance operator or the like so that the maintenance operator or the like can predict the life of the combustible gas detector 22 . By doing so, appropriate measures can be taken, for example, the combustible gas detector 22 is replaced, before the life of the combustible gas detector 22 expires and thereby the fuel cell system 100 fails or stops.
  • the safety of the fuel cell system 100 can be ensured by carrying out the self-diagnostic process involving detecting the life of the combustible gas detector 22 , and by taking appropriate measures.
  • unnecessary maintenance such as inspection and replacement of the combustible gas detector 22 for ensuring the safety of the fuel cell system 100 need not be carried out. Consequently, maintenance cost can be reduced compared to the conventional fuel cell system.
  • FIG. 3 is a view schematically showing a construction of a fuel cell system according to a second embodiment of the present invention.
  • the same reference numerals as those in FIG. 1 of the first embodiment denote the same or corresponding parts, which will not be further described.
  • a branch portion 24 b and a valve 27 b are provided at predetermined positions of the hydrogen-rich gas supply passage 6 connecting the reformer 1 to the anode 8 of the fuel cell stack 7 .
  • the combustible gas guide pipe 23 extends from the branch portion 24 b .
  • a valve 25 b is provided at a predetermined position of the combustible gas guide pipe 23 .
  • Only the raw fuel gas valve 26 is provided at a predetermined position of the raw fuel gas supply passage 4 .
  • the second embodiment is substantially identical to the first embodiment.
  • FIG. 4 is a flowchart showing self-diagnostic steps for the combustible gas detector 22 according to the second embodiment of the present invention.
  • the controller 17 when performing self-diagnostic process as to whether or not the combustible gas detector 22 is functioning properly after determining that the power generation operation is in the stopped state (NO in Step S 6 ), the controller 17 closes the valve 27 b (Step S 7 ), and opens the valve 25 b and the raw fuel gas valve 26 (Step S 8 ). And, the controller 17 injects the raw fuel gas that has flowed through the reformer 1 in small amount toward the combustible gas detector 22 through the combustible gas guide pipe 23 (Step S 9 ).
  • the controller 17 determines that the combustible gas detector 22 is functioning properly, and terminates the self-diagnostic process (YES in Step S 10 ).
  • the controller 17 determines that the combustible gas detector 22 is functioning properly, and terminates the self-diagnostic process (YES in Step S 10 ).
  • the output voltage of the combustible gas detector 22 becomes not higher than the voltage within the proper detection range although the raw fuel gas is injected toward the combustible gas detector 22 (NO in Step S 10 ).
  • the controller 17 recognizes that the combustible gas detector 22 is not functioning properly. And, the controller 17 determines that the life of the combustible gas detector 22 has expired, and takes appropriate safety measures for ensuring safety of the fuel cell system 200 , for example, by displaying information regarding prohibition of the operation of the fuel cell system 200 , displaying a warning, etc (Step S 11 ).
  • the controller 17 when performing the self-diagnostic process after determining that the fuel cell system 200 is carrying out the power generation operation (YES in Step S 6 ), the controller 17 opens the raw fuel gas valve 26 , the valves 25 b and 27 b (Step S 12 ). Under this condition, the controller 17 injects the hydrogen-rich gas which is the combustible gas, in small amount toward the combustible gas detector 22 (Step S 13 ) while supplying the hydrogen-rich gas to the fuel cell stack 7 .
  • the controller 17 determines that the combustible gas detector 22 is functioning properly, and terminates self-diagnostic process (YES in Step S 14 ).
  • the controller 17 determines that the combustible gas detector 22 is functioning properly, and terminates self-diagnostic process (YES in Step S 14 ).
  • the controller 17 determines that the combustible gas detector 22 is functioning properly, and terminates self-diagnostic process (YES in Step S 14 ).
  • the output voltage of the combustible gas detector 22 becomes not higher than the voltage within the proper detection range, although the hydrogen-rich gas is injected toward the combustible gas detector 22 (NO in Step S 14 ).
  • the controller 17 also recognizes that the combustible gas detector 22 is not functioning properly. And, the controller 17 determines that the life of the combustible gas detector 22 has expired, and takes appropriate safety measures for ensuring safety of the fuel cell system 200 , for example, by displaying information regarding prohibition of the operation of the fuel cell system 200 , displaying a warning, etc (Step S 15 ).
  • the raw fuel gas is injected toward the combustible gas detector 22 during the stopped state of the power generation operation of the fuel cell system 200 , while the hydrogen-rich gas is injected toward the combustible gas detector 22 during the power generation operation.
  • the kind of the gas injected toward the combustible gas detector 22 i.e., whether the fuel gas or the hydrogen-rich gas is injected toward the combustible gas detector 22 , is determined based on whether or not the fuel cell system 200 is carrying out the power generation operation. This is because the hydrogen-rich gas is not generated in the reformer 1 in an initial state of an operation of the reformer 1 .
  • the combustible gas detector 22 responds to any kind of combustible gases. But, its detection sensitivity, i.e., the detection output voltage with respect to a predetermined gas concentration varies according to a component (kind) of gases. Accordingly, in order to accurately detect time-lapse degradation of the combustible gas detector 22 , it is necessary to perform the self-diagnostic process for each of kinds of the combustible gases used in the fuel cell system 200 .
  • the self-diagnostic process is carried out using the raw fuel gas before the reforming reaction and the hydrogen-rich gas after the reforming reaction, which may leak into the interior of the package 18 , and it is thus possible to detect degradation of the detection sensitivity of the combustible gas detector 22 to the leakage of these gases, which may occur after an elapse of time.
  • the range of the voltage output from the combustible gas detector 22 varies according to the kind (component) of the injected gases
  • the range of the output voltage is changed according to the kind (component) of the injected gases for the purpose of proper determination. By doing so, the safety of the fuel cell system 200 can be reliably ensured.
  • FIG. 5 is a view schematically showing a construction of a fuel cell system according to a third embodiment of the present invention.
  • the same reference numerals as those in FIG. 1 of the first embodiment denote the same or corresponding parts, which will not be further described.
  • a branch portion 24 c and a valve 27 c are provided at predetermined positions of the exhausted hydrogen passage 10 connecting the anode 8 of the fuel cell stack 7 to the burner 2 .
  • the combustible gas guide pipe 23 extends from the branch portion 24 c .
  • a valve 25 c is provided at a predetermined position of the combustible gas guide pipe 23 .
  • Only the raw fuel gas valve 26 is provided at a predetermined position of the raw fuel gas supply passage 4 .
  • the third embodiment is substantially identical to the first embodiment.
  • FIG. 6 is a flowchart showing self-diagnostic steps for the combustible gas detector 22 according to the third embodiment of the present invention.
  • the controller 17 when performing the self-diagnostic process as to whether or not the combustible gas detector 22 is functioning properly after determining that the fuel cell system 300 is carrying out the power generation operation (YES in Step S 16 ), the controller 17 opens the valve 27 c , the valve 25 c and the raw fuel gas valve 26 (Step S 17 ). And, the controller 17 injects the hydrogen-rich gas that has flowed through the anode 8 of the fuel cell stack 7 , i.e., the hydrogen-rich gas remaining unconsumed after a power generation reaction in the fuel cell stack 7 , in small amount toward the combustible gas detector 22 through the combustible gas guide pipe 23 (Step S 18 ).
  • the controller 17 determines that the combustible gas detector 22 is functioning properly, and terminates the self-diagnostic process (YES in Step S 19 ).
  • the controller 17 determines that the combustible gas detector 22 is functioning properly, and terminates the self-diagnostic process (YES in Step S 19 ).
  • the combustible gas detector 22 has degraded after an elapse of time and the detection sensitivity of the combustible gas detector 22 to the hydrogen-rich gas is low, the output voltage of the combustible gas detector 22 becomes not higher than the voltage within the proper detection range although the hydrogen-rich gas is injected toward the combustible gas detector 22 (NO in Step S 19 ).
  • the controller 17 recognizes that the combustible gas detector 22 is not functioning properly. And, the controller 17 determines that the life of the combustible gas detector 22 has expired, and takes appropriate safety measures for ensuring safety of the fuel cell system 300 , for example, by displaying information regarding prohibition of the operation of the fuel cell system 300 , a warning, etc (Step S 20 ).
  • the controller 17 when performing the self-diagnostic process as to whether or not the combustible gas detector 22 is functioning properly after determining that the power generation operation is in the stopped state (NO in Step S 16 ), first, the controller 17 exhausts the raw fuel gas filled within the fuel cell stack 7 therefrom (Step S 21 ).
  • the controller 17 injects the exhausted raw fuel gas in small amount toward the combustible gas detector 22 through the combustible gas guide pipe 23 (Step S 22 ).
  • the self-diagnostic process regarding the function of the combustible gas detector 22 is performed using the raw fuel gas which is a combustible gas.
  • the controller 17 determines that the combustible gas detector 22 is functioning properly, and terminates the self-diagnostic process (YES in Step S 23 ).
  • the controller 17 recognizes that the combustible gas detector 22 is not functioning properly.
  • the controller 17 determines that the life of the combustible gas detector 22 has expired, and takes appropriate safety measures for ensuring safety of the fuel cell system 300 , for example, by displaying information regarding prohibition of the operation of the fuel cell system 300 , a warning, etc (Step S 24 ).
  • the total exhaust amount of the combustible gas such as the hydrogen-rich gas, the raw fuel gas, and the like can be reduced. Also, in accordance with the third embodiment, the safety of the fuel cell system 300 can be reliably ensured.
  • the reformer is used as a device configured to generate and supply the hydrogen-rich gas, and the hydrogen-rich gas is supplied to the fuel cell stack 7 .
  • the reformer may be replaced by a hydrogen tank which supplies pure hydrogen to the fuel cell stack 7 .
  • the hydrogen tank is used instead of the reformer.
  • FIG. 7 is a view schematically showing a construction of the fuel cell system equipped with the hydrogen tank within the package according to the fourth embodiment of the present invention.
  • the same reference numerals as those in FIG. 1 of the first embodiment denote the same or corresponding parts, which will not be further described.
  • a fuel cell system 400 comprises, within the package 18 , a hydrogen tank 29 which is a hydrogen-rich gas supply means.
  • the hydrogen tank 29 is filled with, for example, compressed hydrogen.
  • one end of the hydrogen-rich gas supply passage 6 is connected to an exit 5 of the hydrogen tank 29 , and the other end thereof is connected to the anode 8 of the fuel cell stack 7 .
  • the branch portion 24 b and the valve 27 b are provided at predetermined positions of the hydrogen-rich gas supply passage 6 .
  • the combustible gas guide pipe 23 is connected to the branch portion 24 b .
  • the valve 25 b is provided at a predetermined position of the combustible gas guide pipe 23 .
  • the hydrogen tank 29 is used as the hydrogen-rich gas supply means in the fourth embodiment, components used to supply the raw fuel gas, for example, the raw fuel gas supply passage 4 , the raw fuel gas valve 26 , the branch portion 24 a , the valve 27 a , and so on, are omitted.
  • the burner 2 of the first to third embodiments is omitted. Because of the absence of the burner 2 , the hydrogen-rich gas remaining unconsumed after the power generation reaction in the fuel cell stack 7 , is exhausted from the fuel cell stack 7 to outside of the fuel cell system 400 through, for example, the exhausted hydrogen passage 10 . Further, since pure hydrogen is supplied to the fuel cell stack 7 in the fourth embodiment, the three-way valves 15 and 16 , and the bypass 14 are omitted. In other respects, the fourth embodiment is substantially identical to the second embodiment.
  • FIG. 8 is a view schematically showing a construction of a fuel cell system equipped with the hydrogen tank outside of the package according to the fourth embodiment of the present invention.
  • the same reference numerals as those in FIG. 1 of the first embodiment denote the same or the corresponding parts, which will not be further described.
  • the fuel cell system 500 of the fourth embodiment is not equipped with the hydrogen tank 29 as the hydrogen-rich gas supply means. Instead, the hydrogen tank 29 is provided outside of the package 18 of the fuel cell system 500 . And, the hydrogen tank 29 is connected to the branch portion 24 b of the fuel cell system 500 through the extended hydrogen-rich gas supply passage 6 .
  • the hydrogen-rich gas supply passage 6 serves as the hydrogen-rich supply means in the fuel cell system 500 .
  • the fuel cell system 500 is identical to the fuel cell system 400 of the fourth embodiment.
  • the fuel cell systems 100 to 500 carries out the self-diagnostic process regarding the detecting function of the combustible gas of the combustible gas detector 22 , it is possible to avoid malfunction or the like of the combustible gas detector 22 .
  • the self-diagnostic process regarding the function of the combustible gas detector 22 can be carried out accurately and reliably.
  • the self-diagnostic process regarding the function of the combustible gas detector 22 can be ideally carried out. With such a configuration, the safety of the fuel cell systems 100 to 500 can be reliably ensured.
  • the present invention is, as a matter of course, applicable to systems equipped with combustible gas detectors within packages thereof, as well as the above-described fuel cell systems. In such systems, the effects provided by the present invention are also obtained.

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US20080075991A1 (en) * 2006-09-25 2008-03-27 Laven Arne Monitoring and control of fuel cell purge to emit non-flammable exhaust streams
US20080145737A1 (en) * 2006-12-19 2008-06-19 General Electric Company Rechargeable fuel cell system
US20090246577A1 (en) * 2008-04-01 2009-10-01 Craft Jr Thomas F Fuel cell cabinet waste water management system
US20090305098A1 (en) * 2006-08-22 2009-12-10 Hideo Ohara Combustion apparatus, combustion processor, and fuel cell generating system
US20090305097A1 (en) * 2008-06-06 2009-12-10 Andreas Kaupert Fuel cell system and motor vehicle equipped therewith
US20100261073A1 (en) * 2007-10-24 2010-10-14 Atomic Energy Council - Institute Of Nuclear Energy Research Solid oxide fuel cell
US20120021313A1 (en) * 2009-01-23 2012-01-26 Shigeki Yasuda Fuel cell system and method for operating the same
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US20140236378A1 (en) * 2011-09-28 2014-08-21 Kyocera Corporation Energy management system, gas meter, and energy management apparatus
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KR100971745B1 (ko) 2007-10-30 2010-07-21 삼성에스디아이 주식회사 연료 전지 시스템 및 그 운전방법
DE102010053572B4 (de) * 2010-12-06 2015-01-15 Enymotion Gmbh Verfahren zum Betrieb eines Brennstoffzellensystems
CN103171407A (zh) * 2011-12-20 2013-06-26 上海汽车集团股份有限公司 氢气强排系统和氢气强排方法
FR2999709B1 (fr) 2012-12-19 2018-11-30 Compagnie Generale Des Etablissements Michelin Detecteur de fuite d'hydrogene
DE102014200938A1 (de) * 2014-01-20 2015-07-23 Bayerische Motoren Werke Aktiengesellschaft Brennstoffzellensystem mit einem in einem Gehäuse integrierten Brennstoffzellenstack
CN103887547B (zh) * 2014-04-23 2016-01-20 北京九谷超微科技有限公司 一种安全控制系统
DE102015207167A1 (de) * 2015-04-21 2016-10-27 Robert Bosch Gmbh Heizsystem, sowie Verfahren zum Betreiben eines Heizsystems
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US8343687B2 (en) * 2006-12-19 2013-01-01 General Electric Company Rechargeable fuel cell system
US20080145737A1 (en) * 2006-12-19 2008-06-19 General Electric Company Rechargeable fuel cell system
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US20120021313A1 (en) * 2009-01-23 2012-01-26 Shigeki Yasuda Fuel cell system and method for operating the same
US20130137006A1 (en) * 2010-12-13 2013-05-30 Panasonic Corporation Power generation system and method of operating the same
US20140236378A1 (en) * 2011-09-28 2014-08-21 Kyocera Corporation Energy management system, gas meter, and energy management apparatus
US9678491B2 (en) * 2011-09-28 2017-06-13 Kyocera Corporation Energy management system, gas meter, and energy management apparatus
US10135079B2 (en) 2012-12-19 2018-11-20 Compagnie Generale Des Etablissements Michelin Fuel cell system equipped with a hydrogen leakage detector

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EP1521325A2 (en) 2005-04-06
CN100511799C (zh) 2009-07-08
US20090263686A1 (en) 2009-10-22
DE602004006686D1 (de) 2007-07-12
DE602004006686T2 (de) 2007-10-04
CN1604378A (zh) 2005-04-06
EP1521325A3 (en) 2005-07-20
US7736815B2 (en) 2010-06-15

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