fuel cell system

Abstract

To reduce impurities of the air supplied to the cathode of a fuel battery stack, by a simple configuration.SOLUTION: A fuel battery system 10A comprises: a fuel battery cell stack 12 that generates electricity from the fuel gas supplied to a fuel electrode 12A and the air supplied to an air electrode 12B; an air supply tube P3 which is provided with an air electrode filter 24 for removing foreign matter, and which introduces the external air having gone through the air electrode filter 24 to the air electrode 12B; a condenser 18 that separates water from an air electrode off-gas discharged from the air electrode 12B; a circulation flow path P9 that supplies the air electrode off-gas after water is separated to the air electrode 12B; and a discharge path P10 to which the air electrode off-gas after water is separated is sent, and which is different from the circulation flow path P9.SELECTED DRAWING: Figure 1

Description

[Technical Field]

[0001] The present invention relates to a fuel cell system. [Background technology]

[0002] Fuel cell systems are sometimes installed in environments where the air contains a large amount of impurities, such as factories and processing facilities. If air containing impurities is continuously supplied to the cathode of the fuel cell stack for power generation, deterioration such as catalyst poisoning and corrosion of component parts in the fuel cell stack will accelerate, potentially leading to system failure or a shortened lifespan.

[0003] Therefore, in Patent Document 1, a filter is provided upstream of the blower that sends air to the fuel cell to remove impurities. However, even with a filter, if the impurity concentration temporarily increases, the amount of impurities that cannot be removed by the filter increases and ends up flowing into the fuel cell. [Prior art documents] [Patent documents]

[0004] [Patent Document 1] Japanese Patent Application Publication No. 2018-10763 Summary of the Invention [Problem to be solved by the invention]

[0005] The present invention has been made in consideration of the above circumstances, and has as its object to reduce impurities in air supplied to an air electrode of a fuel cell with a simple configuration. [Means for solving the problem]

[0006] The fuel cell system of claim 1 comprises a fuel cell that generates electricity using fuel gas supplied to an anode and air supplied to an cathode, an cathode external air inlet path provided with an cathode filter for removing foreign matter and introducing external air that has passed through the cathode filter into the cathode, a water separation unit that separates water from the cathode off-gas discharged from the cathode, a circulation flow path that supplies the cathode off-gas after water has been separated in the water separation unit to the cathode, and an off-gas discharge path that sends the cathode off-gas after water has been separated in the water separation unit to a destination different from the cathode.

[0007] In the fuel cell system according to claim 1, water is separated from the air electrode off-gas discharged from the air electrode in a water separation unit. The air electrode off-gas from which water has been separated is then sent to a circulation flow path that supplies the air electrode and to an off-gas discharge path that is different from the circulation flow path. By sending the air electrode off-gas to the circulation flow path and the off-gas discharge path after water separation in this way, a simpler configuration can be achieved compared to when water is separated in each of the circulation flow path and the off-gas discharge path.

[0008] The air electrode off-gas from which water has been separated is then supplied to the air electrode through the circulation flow path, and the oxygen in the air electrode off-gas is used in the power generation reaction. The air electrode off-gas is obtained by filtering external air from which foreign matter has been removed, and therefore the amount of foreign matter mixed in is reduced. This reduces the amount of new external air used at the air electrode and the amount of impurities flowing into the air electrode.

[0009] In the fuel cell system according to claim 2, the circulation flow path merges with the air electrode external air introduction path downstream of the air electrode filter.

[0010] In this way, by merging the air electrode off-gas with the air electrode external air inlet passage downstream of the air electrode filter, the flow rate of the gas passing through the air electrode filter can be reduced.

[0011] Claim 1The fuel cell system according to the present invention has a combustor that burns a combustible gas, and the circulation flow path supplies the air electrode off-gas and the combustion exhaust gas discharged from the combustor to the air electrode.

[0012] Claim 1 According to the fuel cell system of the present invention, the oxygen in the combustion exhaust gas can also be used in the power generation reaction by supplying the combustion exhaust gas to the air electrode.

[0013] Claim 3 In the fuel cell system according to the above, the off-gas discharge path supplies the air electrode off-gas to the combustor.

[0014] Claim 3 According to the fuel cell system of the present invention, oxygen in the cathode off-gas can be utilized for the combustion reaction in the combustor.

[0015] Claim 4 The fuel cell system according to the above aspect further comprises a circulation flow rate adjusting unit that controls the circulation flow rate of the air electrode off-gas sent to the circulation flow path based on the voltage of the fuel cell during power generation.

[0016] Claim 4 According to the fuel cell system of the present invention, the circulation flow rate adjustment unit controls the circulation flow rate of the cathode off-gas based on the voltage of the fuel cell during power generation, thereby reducing the amount of new external air used at the cathode and reducing the amount of impurities flowing into the cathode. [Effects of the Invention]

[0017] According to the fuel cell system of the present invention, it is possible to reduce impurities in the air supplied to the air electrode of the fuel cell with a simple configuration. [Brief explanation of the drawings]

[0018] [Figure 1] 1 is a configuration diagram of a fuel cell system according to a first embodiment. [Figure 2] FIG. 2 is a configuration diagram of a control unit and related components of the fuel cell system according to the first embodiment. [Figure 3] 10 is an example of a circulation flow rate adjustment table that defines the relationship between voltage and circulation flow rate. [Figure 4] 10 is a flowchart of a circulation adjustment process. [Figure 5] FIG. 10 is a configuration diagram of a fuel cell system according to a second embodiment. [Figure 6] 10 is a flowchart of a circulation control process. [Figure 7] FIG. 10 is a configuration diagram of a fuel cell system according to a third embodiment. [Figure 8] FIG. 10 is a configuration diagram of a fuel cell system according to a fourth embodiment. DETAILED DESCRIPTION OF THE INVENTION

[0019] First Embodiment A first embodiment of the present invention will be described with reference to the drawings.

[0020] The fuel cell system 10A is a power generation system installed in a user's home, an apartment building, a factory, or the like.

[0021] 1 shows an outline of the main components of a fuel cell system 10A according to an embodiment of the present invention. The main components of the fuel cell system 10A according to an embodiment of the present invention include a fuel cell stack 12, a reformer 14, a combustor 16, a condenser 18, a reforming water tank 20, an ion exchange resin 22, an air electrode filter 24, a combustor filter 26, and a control unit 30.

[0022] A raw material gas supply pipe P1 is connected to the reformer 14, and raw material gas is supplied from the raw material gas supply pipe P1 to the reformer 14 by a raw material gas supply blower B1. The raw material gas is not particularly limited as long as it can be reformed, and hydrocarbon fuels can be used. Examples of hydrocarbon fuels include methane, city gas, natural gas, LP gas (liquefied petroleum gas), coal-reformed gas, and lower hydrocarbon gases. Biogas may also be used.

[0023] The reformer 14 reforms the raw material gas to generate fuel gas containing hydrogen. The reformer 14 is connected to the fuel electrode 12A of the fuel cell stack 12. The fuel gas generated in the reformer 14 is supplied to the fuel electrode 12A of the fuel cell stack 12 via a fuel gas pipe P2.

[0024] The fuel cell stack 12 is a cell stack having a plurality of stacked fuel cells. The fuel cell stack 12 is an example of a fuel cell in the present invention, and each fuel cell has an electrolyte layer (not shown), and a fuel electrode 12A and an air electrode 12B stacked on the front and back surfaces of the electrolyte layer, respectively. Note that various fuel cells can be used as the fuel cell stack 12, such as a solid oxide fuel cell (SOFC), a molten carbonate fuel cell (MCFC), and a polymer electrolyte fuel cell (PEFC). In this embodiment, a PEFC will be described as an example.

[0025] One end of an air supply pipe P3 is connected to the air electrode 12B of the fuel cell stack 12, and an air supply blower B2 is connected to the air supply pipe P3. An air electrode filter 24 is provided on the air supply pipe P3 upstream of the air supply blower B2. External air that has passed through the air electrode filter 24 is supplied to the air electrode 12B by the air supply blower B2. The air electrode filter 24 removes foreign matter from the external air. In the fuel cell stack 12, power is generated by a power generation reaction at the fuel electrode 12A and the air electrode 12B, and the power is output to a circuit (not shown). The voltage of the power output to the circuit is detected by a voltage detection unit 13. The voltage detection unit 13 is connected to a control unit 30 (described later) and outputs the detected voltage to the control unit 30.

[0026] Anode offgas is discharged from the anode 12A to anode offgas channel P5, and cathode offgas is discharged from the cathode 12B to anode offgas channel P4. The anode offgas contains fuel gas that has not reacted in the power generation reaction, and this anode offgas is supplied from anode offgas channel P5 to combustor 16 for combustion. The cathode offgas contains oxygen that has not reacted in the power generation reaction and water produced in the power generation reaction. The cathode offgas is combined with combustion exhaust gas, which will be described later, at cathode offgas channel P4 and sent to condenser 18.

[0027] The combustor 16 is provided adjacent to the reformer 14 and heats the reformer 14 with the heat of combustion. One end of a combustion air supply pipe P6 is connected to the combustor 16, and a combustion air supply blower B3 is connected to the combustion air supply pipe P6. A combustor filter 26 is provided on the combustion air supply pipe P6 upstream of the combustion air supply blower B3. External air that has passed through the combustor filter 26 is supplied to the combustor 16 by the combustion air supply blower B3. The combustor filter 26 removes foreign matter from the external air. Anode off-gas is supplied to the combustor 16 from an anode off-gas passage P5, and combustible components in the anode off-gas are combusted by reaction with oxygen contained in the air from the combustion air supply pipe P6.

[0028] One end of a combustion exhaust gas passage P7 is connected to the combustor 16, and the other end of the combustion exhaust gas passage P7 merges with the air electrode off-gas passage P4. The combustion exhaust gas discharged from the combustor 16 merges with the air electrode off-gas (hereinafter, the merged gas is referred to as "mixed gas") and is sent to the condenser 18.

[0029] The other end of the cathode off-gas passage P4 is connected to the condenser 18, where gas-phase water in the mixed gas is condensed and separated into gas and liquid. The liquid-phase water is sent to the reforming water tank 20 via a passage P11. A check valve 11 is provided in the passage P11.

[0030] The mixed gas from which water has been removed is sent to a mixing channel P8. A flow rate regulating three-way valve 19 is provided in the mixing channel P8, and the mixing channel P8 branches into a circulation channel P9 and a discharge channel P10. The downstream end of the circulation channel P9 is connected to the air supply pipe P3 downstream of the air electrode filter 24 and upstream of the air supply blower B2. The discharge channel P10 discharges the mixed gas from which water has been removed to the outside. The flow rate regulating three-way valve 19 is connected to a control unit 30, which will be described later, and adjusts the amount of mixed gas sent to the circulation channel P9 based on a signal from the control unit 30.

[0031] A specified amount of water (liquid phase) is sent to the reforming water tank 20 and stored there, and any amount exceeding the specified amount is discharged to the outside through a discharge pipe P13. The water stored in the reforming water tank 20 is supplied as reforming water to the reformer 14 through the reforming water supply passage P12 and the ion exchange resin 22 by driving the pump 21. The ion exchange resin 22 removes impurities from the passing water by ion exchange.

[0032] 2, the control unit 30 includes, as hardware, a processor 32 and a memory 34. The processor 32 includes a CPU (Central Processing Unit), etc. The memory 34 includes a ROM (Read Only Memory), a RAM (Random Access Memory), and storage, etc.

[0033] The ROM stores various programs and various data. The RAM temporarily stores programs or data as a working area. The storage is composed of an HDD (Hard Disk Drive) or SSD (Solid State Drive), etc., and stores various programs including the operating system and various data. The ROM or storage stores a program for controlling the fuel cell system 10A. The processor 32 reads out the program 35 and executes the program 35 using the RAM as a working area.

[0034] A storage area 36 of the memory 34 stores a circulation flow rate adjustment table T1 (to be described later), voltage data D output from the voltage detection unit 13, operating data of the fuel cell system 10, and the like.

[0035] The circulation flow rate adjustment table T1 is used to adjust the amount of mixed gas (hereinafter referred to as "circulation flow rate C") sent to the circulation flow path P9 in accordance with the voltage data D output from the voltage detection unit 13. As an example, as shown in FIG. 3, the "circulation flow rate C" can be adjusted by starting with a circulation flow rate C1 when the voltage is V2, increasing the circulation flow rate C in proportion to the voltage drop, and adjusting to a circulation flow rate C2 when the voltage is V1. The voltage V2 is set taking into consideration the voltage drop that occurs when foreign matter is mixed in the outside air. In other words, when the voltage V of the voltage data D becomes equal to or lower than V2, it is determined that the device is being affected by foreign matter mixed in the outside air. The voltage V2 is set to a value greater than the voltage V1. Note that the voltage V1 can be set to an abnormally low voltage that exceeds the voltage drop caused by foreign matter mixed in the outside air.

[0036] In addition, an adjustment end voltage V3 is set, and when the voltage V exceeds V3 in the circulation adjustment process described below, this voltage V3 is used as an indicator to stop the supply of the mixed gas to the air electrode 12B. The voltage V3 is set to a value greater than the voltage V2 at which it can be determined that there is no influence from foreign matter mixed in the external air.

[0037] The processor 32 includes, as a functional component, a circulation flow rate adjustment unit 38. The functional components of the circulation flow rate adjustment unit 38 are realized by the processor 32 executing the program 35.

[0038] The operation panel 40 has a display, lamps, switches, etc. The operation panel 40 has switches that can change the operation and settings of the fuel cell system 10A. The communication device 42 is, for example, a modem. The communication device 42 has a function of connecting the fuel cell system 10A to other devices so that they can communicate with each other via the network N.

[0039] Next, the operation of the fuel cell system 10A of this embodiment will be described.

[0040] In the fuel cell system 10A, a raw material gas supply blower B1 sends raw material gas to the reformer 14. In the reformer 14, a fuel gas containing hydrogen is produced from the raw material gas by a reforming reaction. The fuel gas is supplied to the fuel electrode 12A of the fuel cell stack 12 via a fuel gas pipe P2. External air, from which foreign matter has been removed through a cathode filter 24, is supplied to the cathode 12B of the fuel cell stack 12 by an air supply blower B2. In the fuel cell stack 12, the voltage of the power output by the power generation reaction at the fuel electrode 12A and the cathode 12B is detected by a voltage detection unit 13, and the detected voltage is output to a control unit 30. The control unit 30 stores the received voltage data D in a memory area 36.

[0041] In the control unit 30, the circulation adjustment processing program shown in FIG.

[0042] First, in step S10, the latest voltage data D is read from memory area 36, ​​and in step S11, it is determined whether the voltage is V3 or higher. If the voltage is V3 or lower, in step S12, it is determined whether the voltage is V2 or higher. If the voltage is V2 or lower, in step S14, it is determined whether the voltage is V1 or higher. If it is determined that the voltage is lower than V1, it is determined that the voltage is abnormally low, and an abnormality warning is issued in step S20, and the process ends. The abnormality warning can be issued by displaying a warning on operation panel 40, emitting a warning sound, or the like.

[0043] If it is determined in step S14 that the voltage is equal to or greater than V1, it can be determined that the voltage V is being affected by foreign matter mixed in the external air, and the process proceeds to step S16 to reduce the amount of external air being taken in. In step S16, the circulation flow rate adjustment table T1 is referenced to determine the circulation flow rate C corresponding to the read voltage. Then, in step S18, a signal is output to the flow rate adjustment three-way valve 19 to adjust the circulation flow rate C. This allows the mixed gas to be supplied at an appropriate flow rate to the air electrode 12B, and the amount of external air being taken in can be reduced according to the supply rate.

[0044] In step S19, it is determined whether an instruction to end operation has been given, and if an instruction to end operation has been given, the process ends. If operation is to continue, the process returns to step S10 and repeats the process.

[0045] After the determination in step S19 is negative, the process returns to step S10. If it is determined in step S11 that the voltage is greater than V3, the voltage V exceeds the index for stopping the supply of the mixed gas to the air electrode 12B, so in step S13, a signal is output to the flow rate regulating three-way valve 19 to set the circulation flow rate C to zero. Then, the process returns to step S10.

[0046] If the determination in step S19 is negative, the process returns to step S10. If the determination in step S11 is positive and the voltage is determined to be greater than V2 in step S12, the process returns to step S10 without going through step S13 in order to continue supplying the mixed gas to the air electrode 12B.

[0047] In this way, by adjusting the flow rate of the mixed gas sent to the circulation flow path P9 according to the voltage V using the circulation adjustment process, an appropriate flow rate of the mixed gas can be supplied to the air electrode 12B, and the oxygen in the mixed gas can be used at the air electrode 12B. This reduces the amount of external air taken in that corresponds to the amount of mixed gas supplied. Because the mixed gas is made from external air that has had foreign matter removed by a filter, the amount of foreign matter mixed in is reduced. Therefore, the amount of new external air used at the air electrode 12B can be reduced, and the amount of impurities flowing into the air electrode 12B can be reduced.

[0048] In this embodiment, water contained in the mixed gas is removed by the condenser 18 before being supplied to the air electrode 12B, which prevents excess water from flowing into the air electrode 12B. After water separation, the mixed gas is sent to the circulation channel P9 and the discharge channel P10, which allows for a simpler configuration than when water is separated in each of the circulation channel P9 and the discharge channel P10.

[0049] Furthermore, in this embodiment, the air supply pipe P3 joins with the air electrode filter 24 downstream, so the flow rate of the gas passing through the air electrode filter 24 can be reduced.

[0050] Furthermore, in this embodiment, by supplying the combustion exhaust gas to the air electrode 12B, the oxygen in the combustion exhaust gas can also be used in the power generation reaction.

[0051] Second Embodiment Next, a second embodiment of the present invention will be described. In this embodiment, the same parts as in the first embodiment are designated by the same reference numerals, and detailed description thereof will be omitted.

[0052] The fuel cell system 10B of this embodiment is provided with a solenoid valve 44A and an orifice 44B in the circulation flow path P9 instead of the three-way flow rate regulating valve 19 of the fuel cell system 10A of the first embodiment. The configuration other than the solenoid valve 44A and the orifice 44B is the same as that of the fuel cell system 10A of the first embodiment shown in FIG.

[0053] 5, the fuel cell system 10B is provided with a solenoid valve 44A and an orifice 44B in the circulation flow path P9. The solenoid valve 44A is provided upstream of the orifice 44B, and when the solenoid valve 44A is open, the orifice 44B throttles the flow rate of the mixed gas flowing into the circulation flow path P9 to a constant amount. The flow rate of the mixed gas flowing into the circulation flow path P9 is set to a circulation flow rate required by a drop in voltage V. The solenoid valve 44A is connected to the control unit 30, and its opening and closing is controlled by the control unit 30.

[0054] Next, the operation of the fuel cell system 10B of this embodiment will be described.

[0055] In the control unit 30, a circulation control processing program shown in FIG.

[0056] First, steps S10 to S14 are performed in the same manner as in the first embodiment. If it is determined in step S14 that the voltage is equal to or greater than V1, it can be determined that the voltage V is being affected by foreign matter mixed in the external air, and so in order to reduce the amount of external air taken in, the solenoid valve 44A is opened in step S15. This allows the mixed gas to be supplied to the air electrode 12B at a predetermined circulation flow rate, and the amount of external air taken in corresponding to this supply amount can be reduced.

[0057] In step S18, it is determined whether an instruction to end operation has been given, and if an instruction to end operation has been given, the solenoid valve 44A is closed in step S19 and this process ends. If operation is to continue, the process returns to step S10 and repeats the process.

[0058] After the determination in step S18 is negative, the process returns to step S10. If it is determined in step S11 that the voltage is greater than V3, the voltage V exceeds the indicator for stopping the supply of the mixed gas to the air electrode 12B, so in step S17, a signal is output to the solenoid valve 44A to close the solenoid valve 44A. Then, the process returns to step S10.

[0059] If the determination in step S18 is negative, the process returns to step S10. If the determination in step S11 is positive and the voltage is determined to be greater than V2 in step S12, the process returns to step S10 without going through step S17 in order to continue supplying the mixed gas to the air electrode 12B.

[0060] In this way, by controlling whether or not the mixed gas is supplied to the circulation flow path P9 through the circulation control process, the mixed gas can be supplied to the air electrode 12B, and the intake of external air can be reduced by an amount corresponding to the amount of supply.

[0061] <Third embodiment> Next, a third embodiment of the present invention will be described. In this embodiment, the same parts as those in the first and second embodiments are denoted by the same reference numerals, and detailed description thereof will be omitted.

[0062] The fuel cell system 10C of this embodiment differs from the fuel cell system 10A of the first embodiment in that the combustion exhaust gas passage P7 does not merge with the air electrode off-gas passage P4. Other configurations are the same as those of the fuel cell system 10A of the first embodiment shown in FIG.

[0063] 7, the downstream end of the combustion exhaust gas passage P7 is open to the outside, and the combustion exhaust gas is discharged to the outside. Note that before the combustion exhaust gas is discharged to the outside, it may be subjected to heat exchange with the raw material gas, reforming water, etc.

[0064] Similarly to the first embodiment, the fuel cell system 10C of this embodiment also performs a circulation adjustment process (see FIG. 4) during operation. In this way, the circulation adjustment process adjusts the flow rate of the combustion exhaust gas sent to the circulation flow path P9 in accordance with the voltage V, thereby allowing the oxygen in the air electrode off-gas to be used at the air electrode 12B. This makes it possible to reduce the intake of external air in an amount corresponding to the supply amount of combustion exhaust gas.

[0065] <Fourth embodiment> Next, a fourth embodiment of the present invention will be described. In this embodiment, the same parts as those in the first to third embodiments are given the same reference numerals, and detailed descriptions thereof will be omitted.

[0066] The fuel cell system 10D of this embodiment differs from the fuel cell system 10A of the first embodiment in that the downstream end of the air electrode off-gas passage P4 is connected to the combustor 16, the downstream end of the combustion exhaust gas passage P7 is connected to the condenser 18, and the combustion air supply pipe P6 is not provided. Other configurations are the same as those of the fuel cell system 10A of the first embodiment shown in FIG.

[0067] As shown in Figure 8, the downstream end of the flue gas passage P7 is connected to a condenser 18, and the air electrode off-gas is sent from the air electrode 12B to the combustor 16. The oxygen in the air electrode off-gas is used to combustible components in the combustor off-gas. The flue gas from the combustor 16 is sent to the condenser 18 through the flue gas passage P7. In the fuel cell system 10D of this embodiment, water contained in the combustion exhaust gas after the air electrode off-gas is supplied to the combustor 16 is removed by the condenser 18 and then supplied to the air electrode 12B, so that excessive water can be prevented from flowing into the air electrode 12B. After water separation, the exhaust gas is sent to the circulation flow path P9 and the discharge path P10, thereby achieving a simpler configuration than when water is separated in each of the circulation flow path P9 and the discharge path P10.

[0068] Furthermore, since the combustion air supply pipe P6, the combustor filter 26, and the combustion air supply blower B3 are no longer necessary, the number of parts can be reduced.

[0069] The above describes an embodiment of the present invention, but the present invention is not limited to the above, and it goes without saying that the present invention can be implemented in various modified forms within the scope of the gist of the present invention. [Explanation of symbols]

[0070] 10A, 10B, 10C, 10D Fuel Cell Systems 12 Fuel cell stack (fuel cell) 12A fuel electrode 12B Air electrode 16 Combustor 18 Condenser (water separation section) 19 Flow rate adjusting three-way valve (circulation flow rate adjusting part) 24 Air electrode filter 30 Control unit (circulation flow rate adjustment unit) 38 Circulation flow rate adjustment section P3 Air supply pipe P4 Air electrode off-gas passage (air electrode external air inlet passage) P7 Combustion exhaust gas passage P9 Circulation flow path P10 Exhaust path (off gas exhaust path)

Claims

1. a fuel cell that generates electricity using a fuel gas supplied to the fuel electrode and air supplied to the air electrode; an air electrode external air inlet path provided with an air electrode filter for removing foreign matter, and introducing external air into the air electrode through the air electrode filter; a combustor that burns combustible gas; a water separation unit that separates water from the air electrode off-gas discharged from the air electrode and the combustion exhaust gas that has been discharged from the combustor and merged with the air electrode off-gas; a circulation flow path that supplies the air electrode off-gas from which water has been separated in the water separation unit and the combustion exhaust gas to the air electrode; an off-gas discharge path that sends the air electrode off-gas from which water has been separated in the water separation unit to a destination other than the air electrode; A fuel cell system comprising:

2. the circulation flow path is joined with the air electrode external air introduction path downstream of the air electrode filter; The fuel cell system according to claim 1 .

3. the off-gas discharge path supplies the air electrode off-gas to the combustor. The fuel cell system according to claim 2 .

4. The fuel cell further includes a circulation flow rate adjusting unit that controls the circulation flow rate of the cathode off-gas sent to the circulation flow path based on the voltage of the fuel cell during power generation. The fuel cell system according to any one of claims 1 to 3.

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