JP2018170146A - Maintenance device for fuel cell system, fuel cell system, and program - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a fuel cell system maintenance device, a fuel cell system, and a program, capable of coping with priority from an abnormal state having a large influence degree among a plurality of abnormal states generated in a body of the fuel cell system.SOLUTION: A CPU 114 operates as: an execution unit 122 that executes a plurality of processes corresponding to each of a plurality of abnormal states classified according to the degree of influence exerting an influence on a body of a fuel cell system, which is in a plurality of abnormal states generated in the fuel cell system body having a fuel cell stack; and a control unit 124 that controls the execution unit 122 so that corresponding processing among a plurality of processing is executed on the basis of a detection result by a detection unit capable of detecting a plurality of factors each of which can specify occurrence of each of a plurality of abnormal states while priority is given to an abnormal state having a greater influence degree among the plurality of abnormal states.SELECTED DRAWING: Figure 3

Description

  The present invention relates to a maintenance device for a fuel cell system, a fuel cell system, and a program.

  Patent Document 1 discloses a fuel cell system that measures the temperature of a reformed gas in a reformer and corrects an output value of a fuel flow sensor based on a characteristic indicating a relationship between the measured temperature and a fuel flow rate. It is disclosed.

  Patent Document 2 includes a burner that burns off-gas of a fuel gas input to a fuel cell with an oxidant gas, and derives the flow rate of the fuel gas based on a fluctuation value of the flow rate of the oxidant gas supplied to the burner. A fuel cell system is disclosed.

  Patent Document 3 discloses a fuel cell system including a fuel cell that generates power using a reaction gas, a supply unit that supplies the reaction gas to the fuel cell, and a combustion chamber that burns anode off-gas discharged from the fuel cell. Is disclosed. The fuel cell system described in Patent Document 3 is based on the relationship between the combustion chamber temperature index correlated with the temperature of the fuel chamber and the combustion heat amount index correlated with the combustion heat amount in the combustion chamber when the power generation load of the fuel cell is reduced. Thus, the control command value for the reaction gas supply unit is changed.

JP 2010-267450 A JP 2010-257743 A JP 2012-234682 A

  However, in the techniques described in Patent Documents 1 to 3, when a plurality of abnormal states occur in the fuel cell system main body, the abnormal state is dealt with regardless of the degree of influence on the fuel cell system main body. It can be considered. In this case, for example, if an abnormal state of influence that affects the entire fuel cell system main body and an abnormal state of influence that affects only the local area of the fuel cell system main body occur simultaneously, the latter abnormal state takes precedence. May be dealt with. As a result, there is a possibility that the former abnormal state becomes serious and the recovery of the fuel cell system becomes too late.

  The present invention provides a maintenance device for a fuel cell system, a fuel cell system, and a program capable of preferentially dealing with an abnormal state having a large influence among a plurality of abnormal states occurring in a fuel cell system main body. For the purpose.

  In order to achieve the above object, a maintenance device for a fuel cell system according to claim 1 is a plurality of abnormal states occurring in a fuel cell system main body having a fuel cell stack, and the fuel cell system main body includes An execution unit that executes a plurality of processes corresponding to each of a plurality of abnormal states classified according to the degree of influence that has an effect on the plurality of factors, and a plurality of factors that can identify each occurrence of the plurality of abnormal states are detected. Based on the detection result by the possible detection unit, the corresponding process of the plurality of processes is executed in preference to the abnormal state having the larger influence degree among the plurality of abnormal states. And a control unit that controls the execution unit.

  In order to achieve the above object, a fuel cell system according to claim 6 is a fuel cell system having a fuel cell system maintenance apparatus according to any one of claims 1 to 5 and a fuel cell stack. The execution unit included in the maintenance device includes a plurality of abnormal states that occur in the fuel cell system main body, and each of the influence levels affects the fuel cell system main body. A plurality of processes corresponding to each of the classified abnormal states are executed.

  In order to achieve the above object, the program according to claim 7 includes a computer, the execution unit and the control included in the maintenance device for a fuel cell system according to any one of claims 1 to 5. It is a program for functioning as a part.

  According to the present invention, it is possible to preferentially deal with an abnormal state having a large influence among a plurality of abnormal states occurring in the fuel cell system main body.

It is a block diagram which shows an example of the whole structure of the fuel cell system which concerns on embodiment. It is a block diagram which shows an example of a structure of the electric system of the fuel cell system which concerns on embodiment. It is a block diagram which shows an example of a structure of the main control part contained in the control apparatus of the fuel cell system which concerns on embodiment. It is a graph which shows an example of the correlation with the fuel utilization rate shown by the correlation information stored in the control apparatus of the fuel cell system which concerns on embodiment, and the temperature of a combustor. It is a flowchart which shows an example of the flow of the maintenance process which concerns on embodiment. It is a continuation of the flowchart shown in FIG. It is a conceptual diagram which shows an example of the aspect by which a maintenance program is installed in a fuel cell system from the storage medium in which the maintenance program which concerns on embodiment was stored. It is a block diagram which shows the modification of the whole structure of the fuel cell system which concerns on embodiment.

  Hereinafter, an example of an embodiment for carrying out the present invention will be described in detail with reference to the drawings.

  In the following description, “anode” refers to the fuel electrode that is the electrode on the side to which the fuel gas is supplied, and “cathode” refers to the air electrode that is the electrode on the side to which the oxidizing gas is supplied. . In the following description, as an example of the fuel gas, a gas that is used as a fuel and includes hydrogen, hydrocarbons, or the like is employed. In the following description, air is employed as an example of the oxidizing gas.

  In the following description, “match” refers to match in a sense including an error within an allowable range. In the following description, numerical ranges indicated using “to” indicate ranges including numerical values described before and after “to” as the minimum value and the maximum value, respectively.

  As an example, as shown in FIG. 1, the fuel cell system 10 includes a fuel cell system main body 12 and a control device 14 that is an example of a maintenance device for a fuel cell system according to the present invention.

  The fuel cell system body 12 includes a carburetor 16, a reformer 18, a combustor 20, a front fuel cell stack 22, a rear fuel cell stack 24, a tank 26, a pump 28, blowers 30 and 32, a fuel regenerator 34, and An air cooling device 36 is provided. In the following, for convenience of explanation, when it is not necessary to distinguish between the front-stage fuel cell stack 22 and the rear-stage fuel cell stack 24, they are referred to as “fuel cell stacks” without reference numerals.

  In addition, the fuel cell system main body 12 includes a first heat exchange unit 38, a second heat exchange unit 40, a third heat exchange unit 42, and a fourth heat exchange unit 44. The fuel cell system body 12 includes pressure sensors 56, 58, 60, 62, flow sensors 63, 64, 66, voltage sensors 68, 70, temperature sensors 72, 74, 76, 78, 80, 82, 84, 86 and a gas leak sensor 87. Furthermore, the fuel cell system main body 12 includes electromagnetic valves 88, 90, 91.

  The front fuel cell stack 22 includes a cathode 22A and an anode 22B. The rear fuel cell stack 24 includes a cathode 24A and an anode 24B.

  The fuel regenerator 34 includes an inflow portion 50 and a permeation portion 52, and the inflow portion 50 and the permeation portion 52 are partitioned by a separation membrane 92.

  One end of a source gas pipe P1, which is a pipe through which source gas flows, is connected to the vaporizer 16, and the other end of the source gas pipe P1 is connected to the blower 30. The blower 30 supplies the raw material gas to the vaporizer 16 by sending the raw material gas to the vaporizer 16 through the raw material gas pipe P1.

  Further, one end of a water supply pipe P2 that is a pipe through which water flows is connected to the vaporizer 16, and the other end of the water supply pipe P2 is connected to the tank 26. Water is stored in the tank 26.

  The pump 28 pumps water from the tank 26 via the water supply pipe P2. Then, the pump 28 supplies the water to the vaporizer 16 by sending the pumped water to the vaporizer 16 through the water supply pipe P2.

  The vaporizer 16 vaporizes the water supplied from the water supply pipe P2. For the vaporization, heat from the combustor 20 or the like is used. In the present embodiment, methane is adopted as an example of the raw material gas. However, the gas is not particularly limited as long as it can be reformed, and a hydrocarbon fuel can be used. Examples of the hydrocarbon fuel include natural gas, LP gas (liquefied petroleum gas), coal reformed gas, lower hydrocarbon gas, and the like. Examples of the lower hydrocarbon gas include lower hydrocarbons having 4 or less carbon atoms such as methane, ethane, ethylene, propane, and butane, and methane used in the present embodiment is preferable. The hydrocarbon fuel may be a mixture of the above-described lower hydrocarbon gas, and the above-mentioned lower hydrocarbon gas is a gas such as natural gas, city gas, LP gas, biogas, etc. Also good.

  The vaporizer 16 supplies the raw material gas and water vapor to the reformer 18 by sending the raw material gas and water vapor to the reformer 18 through the pipe P3.

  The reformer 18 is adjacent to the combustor 20, the front stage fuel cell stack 22, and the rear stage fuel cell stack 24, and exchanges heat between the combustor 20, the front stage fuel cell stack 22, and the rear stage fuel cell stack 24. You may heat by performing.

  The reformer 18 reforms the raw material gas and generates a fuel gas having a temperature of about 600 ° C. containing hydrogen. The reformer 18 is connected to the anode 22B. The fuel gas generated by the reformer 18 is supplied to the anode 22B through the fuel gas pipe P4.

  The front fuel cell stack 22 is a solid oxide fuel cell stack, and has a plurality of stacked fuel cells. The operating temperature of the front fuel cell stack 22 is about 500 ° C. or higher. Each fuel cell includes an electrolyte layer, and a cathode 22A and an anode 22B that are respectively stacked on the front and back surfaces of the electrolyte layer. In the example shown in FIG. 1, individual cathodes of a plurality of fuel cells are collectively shown as “cathode 22A”, and individual anodes of the plurality of fuel cells are collectively shown as “anode 22B”. .

  One end of an oxidizing gas pipe P5, which is a pipe through which oxidizing gas flows, is connected to the cathode 22A. The oxidizing gas is supplied to the cathode 22A through the oxidizing gas pipe P5. In the cathode 22A, as shown in the following formula (1), oxygen and electrons in the oxidizing gas react to generate oxygen ions. The generated oxygen ions reach the anode 22B through the electrolyte layer.

(Air electrode reaction) 1 / 2O ₂ + 2e ⁻ → O ²⁻ (1)

  On the other hand, in the anode 22B, as shown in the following formulas (2) and (3), oxygen ions that have passed through the electrolyte layer react with hydrogen and carbon monoxide in the fuel gas, and water (water vapor), carbon dioxide , And electrons are generated. Electrons generated at the anode 22B move from the anode 22B through the external circuit to the cathode 22A, thereby generating electric power in each fuel cell. Each fuel cell generates heat during power generation.

(Fuel electrode reaction) H ₂ + O ²⁻ → H ₂ O + 2e ⁻ (2)

CO + O ²⁻ → CO ₂ + 2e ⁻ (3)

  One end of an anode offgas pipe P6 that is a pipe through which the anode offgas flows is connected to the anode 22B, and the anode offgas is discharged from the anode 22B to the anode offgas pipe P6. The anode off gas contains unreacted hydrogen, unreacted carbon monoxide, carbon dioxide, water vapor, and the like.

  Note that the fuel cell is not limited to a solid oxide fuel cell (SOFC), and other fuel cells in which at least one of carbon dioxide and hydrogen is contained in the anode off-gas, such as molten carbon dioxide. It may be a salt fuel cell (MCFC).

  One end of a cathode offgas pipe P13 that is a pipe through which the cathode offgas flows is connected to the cathode 22A, and the cathode offgas is discharged from the cathode 22A to the cathode offgas pipe P13.

  The other end of the anode off gas pipe P6 is connected to the inflow part 50 through the fourth heat exchange part 44 and the first heat exchange part 38.

  The anode off gas discharged from the anode 22B flows into the inflow portion 50, and the fuel regenerator 34 separates carbon dioxide and water vapor from the anode off gas flowing into the inflow portion 50.

  The transmission part 52 is interposed in the middle of the oxidizing gas pipe P5 on the upstream side of the branch part B2 of the oxidizing gas pipe P5. The blower 32 is connected to the other end of the oxidizing gas pipe P5. The blower 32 supplies the oxidizing gas as a sweep gas to the permeation unit 52 by sending the oxidizing gas at room temperature to the oxidizing gas pipe P2.

  The separation membrane 92 has a function of transmitting at least one of carbon dioxide and water vapor.

  In the permeation section 52, the oxidizing gas supplied from the oxidizing gas pipe P5 flows into the permeation section 52 as a sweep gas. As a result, the partial pressure of carbon dioxide in the permeation section 52 decreases, and carbon dioxide or the like easily moves to the permeation section 52 through the separation membrane 92 from the inflow section 50. The oxidizing gas is sent out from the permeation section 52 as permeation section exhaust gas together with carbon dioxide, water vapor, and other gas in the anode off-gas that has passed through the separation membrane 92. The permeable portion exhaust gas sent from the permeable portion 52 is supplied to the cathode 22A as an oxidizing gas containing oxygen through the oxidizing gas pipe P5.

  The anode off-gas is separated from the carbon dioxide and water vapor by the separation membrane 92, so that the concentration of carbon dioxide and water vapor is reduced, and becomes a regenerated fuel gas, which is sent out from the inflow portion 50. One end of the regenerated fuel gas pipe P7-1, which is a pipe through which the regenerated fuel gas flows, is connected to the outlet of the inflow portion 50, and the other end of the regenerated fuel gas pipe P7-1 is connected to the air cooling device 36. Yes. Accordingly, the regenerated fuel gas sent from the inflow portion 50 is supplied to the air cooling device 36 via the regenerated fuel gas pipe P7-1.

  The air cooling device 36 cools the regenerated fuel gas supplied from the inflow portion 50. One end of the regenerated fuel gas pipe P7-2, which is a pipe through which the regenerated fuel gas flows, is connected to the discharge port of the air cooling device 36, and the other end of the regenerated fuel gas pipe P7-2 is in a state where water is stored. It is inserted in the tank 26.

  The air cooling device 36 supplies the cooled regenerated fuel gas to the tank 26 by sending it to the regenerated fuel gas pipe P7-2. The water obtained by condensation by the cooling operation in the air cooling device 36 is discharged to the tank 26 and stored in the tank 26.

  The basic configuration of the rear stage fuel cell stack 24 is the same as that of the front stage fuel cell stack 22, and the rear stage fuel cell stack 24 includes a cathode 24A corresponding to the cathode 22A and an anode 24B corresponding to the anode 22B.

  One end of the regenerated fuel gas pipe P8, which is a pipe through which the regenerated fuel gas flows, is inserted into the tank 26 without touching the water in the tank 26, and the other end of the regenerated fuel gas pipe P8 is connected to the anode 24B. It is connected. The other end of the cathode offgas pipe P13 is connected to the cathode 24A, and the cathode offgas discharged from the cathode 22A via the cathode offgas pipe P13 is supplied to the cathode 22A. Accordingly, in the rear fuel cell stack 24, power is generated by each fuel cell by the same reaction as that of the front fuel cell stack 22, and each fuel cell generates heat during power generation.

  Thus, in the fuel cell system 10, first, fuel gas is used by the front fuel cell stack 22 as fuel to be used for power generation in the front fuel cell stack 22, thereby generating power in the front fuel cell stack 22. Next, after the fuel gas is used by the front fuel cell stack 22, the anode off-gas discharged from the front fuel cell stack 22 is regenerated as a regenerated fuel gas by the fuel regenerator 34. Then, the regenerated fuel gas is used as fuel in the rear fuel cell stack 24, thereby generating electric power in the rear fuel cell stack 24.

  One end of the pipe P9 is connected to the cathode 24A, and the other end of the pipe P9 is connected to the combustor 20. Therefore, the used gas discharged from the cathode 24A is supplied to the combustor 20 by being sent to the pipe P9.

  One end of the pipe P10 is connected to the anode 24B, and the other end of the pipe P10 is connected to the combustor 20. Therefore, the used gas discharged from the anode 24B is supplied to the combustor 20 by being sent to the pipe P10.

  The combustor 20 uses the used gas supplied from the cathode 24A and the anode 24B for incineration.

  One end of the pipe P11 is connected to the combustor 20. A middle portion of the pipe P11 is disposed in the vaporizer 16, and in the vaporizer 16, water is vaporized by heat of the pipe P11. The other end of the pipe P11 protrudes from the vaporizer 16 to the outside of the vaporizer 16. The combustion exhaust gas which is the gas discharged from the combustor 20 is discharged to the outside through the vaporizer 16 by being sent to the pipe P11.

  The first heat exchange unit 38 is provided at a midpoint P6A that is a midpoint of the anode off-gas pipe P6 and a midpoint P5A that is a midpoint of the oxidizing gas pipe P5. The midpoint P6A refers to a location downstream of the junction I1 and upstream of the inlet 50 with respect to the anode offgas pipe P6. The midpoint P5A refers to a location downstream of the branching section B2 and upstream of the transmission section 52 with respect to the oxidizing gas pipe P5.

  In the first heat exchanging unit 38, heat exchange is performed between the anode off gas flowing through the anode off gas pipe P6 and the oxidizing gas flowing through the oxidizing gas pipe P5. After the anode off gas is delivered from the anode 22B, the temperature is lower than that at the time of delivery from the anode 22B due to heat exchange in the fourth heat exchange section 44 described later.

  The second heat exchanging unit 40 is provided at a midpoint P5B that is a midpoint of the oxidizing gas pipe P5 and a midpoint P11A that is a midpoint of the pipe P11. The midpoint P5B refers to a location upstream of the branch portion B2 and downstream of the midpoint P5A in the oxidizing gas pipe P5. The halfway point P11A indicates a point between the combustor 20 and the vaporizer 16 with respect to the pipe P11. In the second heat exchange unit 40, heat exchange is performed between the oxidizing gas flowing through the oxidizing gas pipe P5 and the combustion exhaust gas flowing through the pipe P11.

  The third heat exchanging unit 42 is provided at a midpoint P5C that is a midpoint of the oxidizing gas pipe P5 and a midway location P11B that is a midpoint of the pipe P11. The midpoint P5C refers to a location upstream of the permeable portion 52 and downstream of the blower 32 with respect to the oxidizing gas pipe P5. The midpoint P11B refers to a location upstream of the vaporizer 16 and downstream of the midpoint 11A with respect to the pipe P11. In the 3rd heat exchange part 42, heat exchange is performed between the oxidizing gas which flows through the oxidizing gas pipe P5, and the combustion exhaust gas which flows through the piping P11.

  The fourth heat exchanging portion 44 is provided at a midpoint P6B that is a midpoint of the anode off-gas pipe P6 and a midpoint P8A that is a midpoint of the regenerated fuel gas pipe P8. The midpoint P6B refers to a location upstream of the midpoint P6A and downstream of the anode 22B in the anode off gas pipe P6. The midpoint P8A refers to a location upstream of the anode 24B and downstream of the tank 26 with respect to the regenerated fuel gas pipe P8. In the fourth heat exchanging unit 44, heat exchange is performed between the anode off gas flowing through the anode off gas pipe P6 and the regenerated fuel gas flowing through the regenerated fuel gas pipe P8.

  One end of a bypass pipe P12, which is a bypass pipe through which the anode off-gas flows, is connected to a midpoint P6C, which is a midpoint of the anode offgas pipe P6, and the other end of the bypass pipe P12 is connected to the regenerated fuel gas pipe P8. It is connected to a midpoint P8B that is a midway location. Here, the midpoint P6C refers to a location upstream of the inflow portion 50 and downstream of the midpoint P6A with respect to the anode offgas pipe P6. The midpoint P8B refers to a location upstream of the midpoint P8A and downstream of the tank 26 with respect to the regenerated fuel gas pipe P8.

  The electromagnetic valve 88 is provided in the bypass pipe P12. The electromagnetic valve 90 is provided upstream of the inflow portion 50 and downstream of the midway location P6C with respect to the anode off-gas pipe P6. The electromagnetic valve 91 is provided on the upstream side of the midway location P8B with respect to the regenerated fuel gas pipe P8. The electromagnetic valve 88 opens and closes the bypass pipe P12 under the control of the control device 14. The electromagnetic valve 90 opens and closes the anode off gas pipe P6 under the control of the control device 14. The electromagnetic valve 91 opens and closes the regenerated fuel gas pipe P8 under the control of the control device 14.

  The pressure sensor 56 is provided in the source gas pipe P1, and detects the pressure of the source gas in the source gas pipe P1. The pressure sensor 58 is provided upstream of the midpoint P5C and downstream of the blower 32 with respect to the oxidizing gas pipe P5, and detects the pressure of the oxidizing gas in the oxidizing gas pipe P5. The pressure sensor 60 is provided on the upstream side of the permeable portion 52 and on the downstream side of the midway location P5C with respect to the oxidizing gas pipe P5, and detects the pressure of the oxidizing gas in the oxidizing gas pipe P5. . The pressure sensor 62 is provided between the anode 22B and the anode 24B. As an example, the pressure sensor 62 is provided upstream of the midway location P8B and downstream of the tank 26 with respect to the regenerated fuel gas pipe P8. The pressure of the regenerated fuel gas in the regenerated fuel gas pipe P8 is detected.

  The flow sensor 63 is provided upstream of the vaporizer 16 and downstream of the pump 28 with respect to the water supply pipe P <b> 2, and detects the flow rate of water flowing into the vaporizer 16. The flow sensor 64 is provided on the upstream side of the vaporizer 16 and on the downstream side of the pressure sensor 56 with respect to the raw material gas pipe P1, and detects the flow rate of the raw material gas in the raw material gas pipe P1. . The flow sensor 66 is provided on the upstream side with respect to the oxidizing gas pipe P5 and on the downstream side of the pressure sensor 58, and detects the flow rate of the oxidizing gas in the oxidizing gas pipe P5. .

  The voltage sensor 68 is provided between the cathode 22A and the anode 22B, and detects the voltage at the cathode 22A and the anode 22B. The voltage sensor 70 is provided between the cathode 24A and the anode 24B, and detects the voltage at the cathode 24A and the anode 24B.

  The temperature sensor 72 is provided in the front fuel cell stack 22 and detects the temperature in the front fuel cell stack 22. The temperature sensor 74 is provided in the rear fuel cell stack 24 and detects the temperature of the space around the cathode 24A and the anode 24B. The temperature sensor 76 is provided in the combustor 20 and detects the combustion temperature in the combustor 20. The temperature sensor 78 is provided in the vaporizer 16 and detects the temperature in the vaporizer 16. The temperature sensor 80 is provided in the reformer 18 and detects the temperature in the reformer 18. The temperature sensor 82 is provided in the regenerated fuel gas pipe P7-1, and detects the temperature of the regenerated fuel gas flowing through the regenerated fuel gas pipe P7-1. The temperature sensor 84 is provided upstream of the vaporizer 16 and downstream of the flow sensor 63 with respect to the water supply pipe P <b> 2, and detects the temperature of the water flowing into the vaporizer 16. The temperature sensor 86 is provided downstream of the vaporizer 16 (the other end side of the pipe P11) with respect to the pipe P11, and detects the temperature of the combustion exhaust gas.

  The gas leak sensor 87 detects leaked gas that is leaked to the outside from the fuel regenerator 34. The leakage gas refers to, for example, a gas contained in the regenerated fuel gas and a gas contained in the anode off gas. In the present embodiment, the gas leak sensor 87 detects the leaked gas by detecting a concentration equal to or higher than a reference value for each of the gas contained in the regenerated fuel gas and the gas contained in the anode off gas.

  As an example, as illustrated in FIG. 2, the control device 14 includes a main control unit 100, a reception interface (I / F) 102, a reception device 104, a display control unit 106, a display 108, a bus line 110, and a communication I / F 112. Including.

  Each of the main control unit 100, the reception I / F 102, the display control unit 106, and the communication I / F 112 is connected to the bus line 110. Accordingly, the main control unit 100 exchanges various information with each of the reception I / F 102 and the display control unit 106.

  The reception device 104 has a keyboard, a mouse, a touch panel, and the like, and receives various instructions from the user. The reception device 104 is connected to the reception I / F 102 and outputs an instruction content signal indicating the content of the received instruction to the reception I / F 102. The main control unit 100 executes processing according to the instruction content signal input from the reception I / F 102.

  The display 108 is, for example, an LCD (Liquid Crystal Display) or an OELD (Organic Electroluminescence Display). The display 108 is connected to the display control unit 106. The display control unit 106 displays various screens such as a menu screen by controlling the display 108 under the control of the main control unit 100.

  The communication I / F 112 is connected to the electrical system of the fuel cell system main body 12, operates under the control of the main control unit 100, and between the main control unit 100 and the electrical system of the fuel cell system main body 12. It is responsible for sending and receiving various information.

  The fuel cell system main body 12 includes a detector 113, a blower drive circuit 130, a pump drive circuit 132, a rotation speed detector 134, a blower group 136, an electromagnetic valve drive circuit 137, and an electromagnetic valve group 139.

  The detection unit 113 is a set of a plurality of sensors capable of detecting a plurality of factors. Here, the plurality of factors refers to a plurality of factors capable of specifying each occurrence of a plurality of abnormal states occurring in the fuel cell system main body 12. In addition, “a plurality of abnormal states” refers to a plurality of abnormal states classified by the degree of influence that affects the fuel cell system main body 12. “Influence” refers to, for example, at least one of the influence on the safety of the fuel cell system main body 12 and the influence on the operation of the fuel cell system main body 12. Here, “operation of the fuel cell system main body 12” refers to an operation capable of realizing the power generation efficiency as designed.

  Here, if the degree of influence on “operation of the fuel cell system main body 12” is expressed as “large” and “small”, the degree of influence “large” means, for example, that the power generation efficiency is less than a preset threshold value. Means influence. The influence degree “small” means, for example, an influence degree in which the power generation efficiency is equal to or higher than a preset threshold value, but is less than a lower limit value of a range preset as a standard range of power generation efficiency. Even if the degree of influence is “low”, the degree of influence gradually increases as the power generation efficiency approaches a preset threshold value.

  Hereinafter, for convenience of explanation, the plurality of abnormal states described above are referred to as “a plurality of abnormal states in the fuel cell system main body 12” or “a plurality of abnormal states”.

  The detection unit 113 includes a voltage sensor group 113A, a temperature sensor group 113B, a flow rate sensor group 113C, a pressure sensor group 113D, and a gas leak sensor 87.

  The voltage sensor group 113A indicates a set of a plurality of voltage sensors including at least the voltage sensors 68 and 70. The temperature sensor group 113B refers to a set of temperature sensors including at least the temperature sensors 72, 74, 76, 78, 80, 82, 84, 86. The flow sensor group 113C indicates a set of a plurality of flow sensors including at least the flow sensors 63, 64, and 66. The pressure sensor group 113D indicates a set of a plurality of pressure sensors including at least the pressure sensors 56, 58, 60, and 62.

  The pressure detected by the voltage sensor group 113D is an example of a factor according to the present invention. The temperature detected by the temperature sensor group 113B is also an example of the factor according to the present invention. The flow rate detected by the flow rate sensor group 113C is also an example of the factor according to the present invention. The pressure detected by the pressure sensor group 113D is also an example of the factor according to the present invention. Furthermore, the leaked gas detected by the gas leak sensor 87 is an example of the factor according to the present invention.

  The voltage sensor group 113A, the temperature sensor group 113B, the flow sensor group 113C, the pressure sensor group 113D, and the gas leak sensor 87 are connected to the communication I / F 112. The main control unit 100 acquires voltage information, temperature information, flow rate information, pressure information, and gas leakage information.

  Here, the voltage information refers to information indicating a detection result by the voltage sensor group 113A. The voltage information is roughly classified into first voltage information indicating the voltage detected by the voltage sensor 68 and second voltage information indicating the voltage detected by the voltage sensor 70.

  The temperature information indicates a detection result by the temperature sensor group 113B. The temperature information is roughly divided into first to eighth temperature information. The first temperature information refers to information indicating the temperature detected by the temperature sensor 72. The second temperature information refers to information indicating the temperature detected by the temperature sensor 74. The third temperature information refers to information indicating the temperature detected by the temperature sensor 76. The fourth temperature information refers to information indicating the temperature detected by the temperature sensor 78. The fifth temperature information refers to information indicating the temperature detected by the temperature sensor 80. The sixth temperature information refers to information indicating the temperature detected by the temperature sensor 82. The seventh temperature information refers to information indicating the temperature detected by the temperature sensor 84. The eighth temperature information refers to information indicating the temperature detected by the temperature sensor 86.

  The flow rate information refers to information indicating a detection result by the flow rate sensor group 113C. The flow rate information includes first flow rate information indicating the flow rate detected by the flow rate sensor 64, second flow rate information indicating the flow rate detected by the flow rate sensor 66, and third flow rate information indicating the flow rate detected by the flow rate sensor 63. It is roughly divided into

  The pressure information refers to information indicating a detection result by the pressure sensor group 113D. The pressure information is roughly divided into first to fourth pressure information. The first pressure information refers to information indicating the pressure detected by the pressure sensor 56. The second pressure information refers to information indicating the pressure detected by the pressure sensor 58. The third pressure information refers to information indicating the pressure detected by the pressure sensor 60. The fourth pressure information indicates information indicating the pressure detected by the pressure sensor 62.

  The gas leak information is information indicating whether or not leaked gas is detected by the gas leak sensor 87.

  The blower group 136 is a set of a plurality of blowers including the blowers 30 and 32 that are used in the fuel cell system main body 12. The blower drive circuit 130 is connected to the communication I / F 112 and the blower group 136, and controls the blower group 136 in accordance with an instruction from the main control unit 100.

  The pump drive circuit 132 is connected to the communication I / F 112 and the pump 28, and controls the pump 28 in accordance with an instruction from the main control unit 100.

  The rotation speed detection unit 134 detects the rotation speed of the pump 28 and outputs rotation speed information indicating the detected rotation speed. An example of the rotation speed detection unit 134 is a rotary encoder. The rotation speed detection unit 134 is connected to the communication I / F 112. The main control unit 100 acquires the rotation speed information from the rotation speed detection unit 134 via the communication I / F 112. In this embodiment, rpm (revolution per minute) is adopted as an example of the unit of the rotation speed of the pump 28, but this unit is merely an example.

  In addition, here, a method of directly detecting the rotation speed by the rotation speed detection unit 134 is illustrated, but the present invention is not limited to this. For example, the rotational speed may be calculated from a value such as a voltage value that commands the rotational speed to the pump. Moreover, although the rotation speed of the pump 28 is illustrated here, the present invention is not limited to this. For example, the present invention can be realized by using the flow rate of water measured by the flow rate sensor 63 instead of the rotational speed of the pump 28. For example, at least one of the determination as to whether or not a pump abnormal state described later has occurred and the pump handling process may be performed based on the flow rate of water measured by the flow sensor 63. The main control unit 100 can easily grasp the amount of water by using the measurement result obtained by the flow sensor 63 as compared with the case where the rotation speed of the pump 28 is used.

  The solenoid valve group 139 is a set of a plurality of solenoid valves including the solenoid valves 88 and 90 that are used in the fuel cell system main body 12. The solenoid valve drive circuit 137 is connected to the communication I / F 112 and the solenoid valve group 139, and controls the solenoid valve group 139 in accordance with an instruction from the main control unit 100.

  As an example, as illustrated in FIG. 3, the main control unit 100 includes a CPU (Central Processing Unit) 114, a primary storage unit 116, and a secondary storage unit 118, and the CPU 114, the primary storage unit 116, and the secondary storage unit 118. Are connected to the bus line 110.

  The CPU 114 controls the entire fuel cell system 10. The primary storage unit 116 is a volatile memory used as a work area when various programs are executed. An example of the primary storage unit 116 is a RAM (Random Access Memory). The secondary storage unit 118 is a non-volatile memory that stores a program for controlling basic operations of the fuel cell system 10, various parameters, and the like. As an example of the secondary storage unit 118, an EEPROM (Electrically Erasable) is used. Programmable Read Only Memory), flash memory, and the like.

  The secondary storage unit 118 stores a maintenance program 120 and a plurality of correlation information 121. The CPU 114 operates as the execution unit 122 and the control unit 124 by reading the maintenance program 120 from the secondary storage unit 118, developing it in the primary storage unit 116, and executing the maintenance program 120.

  The execution unit 122 executes a plurality of processes respectively corresponding to a plurality of abnormal states. Based on the detection result of the detection unit 113, the control unit 124 prioritizes the abnormal state having a larger influence on the fuel cell system main body 12 out of the plurality of abnormal states, and performs a plurality of processes. The execution unit 122 is controlled so that the corresponding process is executed.

  As an example, as shown in FIG. 4, the correlation information 121 is information indicating a predetermined correlation between the combustion temperature and the fuel utilization rate. The combustion temperature is the combustion temperature in the combustor 20. Here, the predetermined correlation is, for example, a correlation between the combustion temperature and the fuel utilization rate that can realize the power generation efficiency within a range set in advance as a standard range of the power generation efficiency. -A correlation determined in advance based on results obtained from simulation or the like.

  The fuel utilization rate is calculated based on the flow rate of the raw material gas and the amount of current in the fuel cell stack. For example, the fuel utilization rate is calculated by the following equation (4). The amount of current in the fuel cell stack is used to calculate “amount of source gas used for reaction” in the following equation (4).

  (Fuel utilization rate) = (Amount of raw material gas used for reaction) / (Flow rate of raw material gas) (4)

  The correlation information 121 is determined for each combination of the amount of current in the fuel cell stack, the combustion temperature, and the flow rate of the raw material gas, for example.

  Next, as an operation of the portion of the fuel cell system 10 according to the present invention, the maintenance process executed by the CPU 114 by the CPU 114 following the maintenance program 120 after the operation of the fuel cell system 10 is started will be described with reference to FIGS. The description will be given with reference.

  The plurality of abnormal states in the fuel cell system main body 12 are roughly classified into a supply system abnormal state and a non-supply system abnormal state. The supply system abnormal state is an abnormal state related to a supply system that supplies a fluid to be supplied to the power generation of the fuel cell stack to a supplied part included in the fuel cell system main body 12. The non-supply system abnormal state is an abnormal state different from the supply system abnormal state among a plurality of abnormal states in the fuel cell system main body 12. In addition, the non-supply system abnormal state does not affect the fuel cell system main body 12 immediately or an abnormal state in which the influence degree affecting the fuel cell system main body 12 is smaller than the supply system abnormal state. An abnormal condition.

  Here, the above-mentioned “fluid for power generation of the fuel cell stack” refers to a basic raw material fluid, for example. The basic raw material fluid refers to a fluid corresponding to a basic raw material used for power generation of the fuel cell stack. Examples of basic raw material fluids include raw material gas, oxidizing gas, and water, and differ depending on the type of fuel cell stack and the system configuration. In the fuel cell system 10, a secondary raw material fluid is also used. The secondary raw material fluid refers to a fluid corresponding to a secondary raw material used for power generation of the fuel cell stack. Examples of the secondary feed fluid include regenerated fuel gas and sweep gas.

  The above “supplied portion” refers to a component to which a basic raw material fluid is supplied by a supply system among all the components of the fuel cell system main body 12. Examples of the “supplied part” include a vaporizer 16, a fuel cell stack, and a reformer 18.

  The above-mentioned “supply system” refers to a component that directly contributes to supplying the basic raw material fluid to the supply target part by sending out the basic raw material fluid among the constituent members of the fuel cell system main body 12. In other words, the “supply system” means, for example, at least one abnormal state of a pump abnormal state, a raw material gas system abnormal state, and an oxidizing gas system abnormal state, which will be described later, among all the constituent members of the fuel cell system main body 12. It refers to a component that can be a direct factor that causes the occurrence of. An example of the “supply system” includes the pump 28 and the blowers 30 and 32.

  The maintenance process according to the present embodiment is a process including a supply system maintenance process and a non-supply system maintenance process. The supply system maintenance process refers to a process corresponding to a supply system abnormal state. In the example shown in FIG. 5, the supply system maintenance process is a process from step 202 to step 214. The non-supply system maintenance process refers to a process corresponding to a non-supply system abnormal state. In the example shown in FIG. 6, the non-supply system maintenance process is a process from step 220 to step 244.

  In the maintenance process illustrated in FIG. 5, in step 200, the control unit 124 causes the execution unit 122 to perform a plurality of corresponding processes (see steps 206, 210, 214, 224, 228, 232, 236, 240, and 244) described later. It is determined whether at least one of the above is being executed. The "multiple handling processes" mentioned here are pump handling, source gas handling, oxidation gas handling, front external leak handling, front internal leak handling, gas leak handling, deterioration handling, Refers to external leak handling processing and subsequent internal leak handling processing.

  In step 200, when the execution unit 122 is executing at least one of the plurality of corresponding processes, the determination is affirmed and the process proceeds to step 216. When the execution unit 122 is not executing any of the plurality of corresponding processes in Step 200, the determination is negative and the process proceeds to Step 202.

  In step 216, the control unit 124 determines whether or not a corresponding process end condition that is a condition for ending the currently executed corresponding process is satisfied. An example of the response process end condition is a condition that the reception device 104 has received an instruction to end the currently executed response process.

  In step 216, if the response processing end condition is satisfied, the determination is affirmed and the process proceeds to step 218. If it is determined in step 216 that the response processing end condition is not satisfied, the determination is negative and the routine proceeds to step 200.

  In step 218, the control unit 124 causes the execution unit 122 to end the execution of the currently executed corresponding process, and then proceeds to step 202.

  In step 202, the control unit 124 acquires supply system factor information, and then proceeds to step 204.

  Here, the supply system factor information refers to information indicating a factor used for specifying occurrence of a supply system abnormal state. In this step 202, rotation speed information and flow rate information are adopted as an example of supply system factor information.

  In step 204, the control unit 124 determines whether or not a pump abnormal state in which an element related to the pump 28 is in an abnormal state has occurred based on the rotation speed information acquired in the process of step 202. The element related to the pump 28 refers to an element that directly or indirectly affects the normal operation of the pump 28, for example. The elements that directly or indirectly affect the normal operation of the pump 28 include, for example, at least one of the pump 28 itself and an electric system between the pump 28 and the communication I / F 112. Point to one.

  For example, in step 204, it is determined that a pump abnormal state has occurred when the rotation speed of the pump 28 indicated by the rotation speed information acquired in the process of step 202 is not included in the first predetermined range. In step 204, it is determined that the pump abnormal state has not occurred when the rotation speed of the pump 28 indicated by the rotation speed information acquired in the process of step 202 is included in the first predetermined range. Note that the first predetermined range refers to a range determined in advance by a test using an actual machine, computer simulation, or the like as a range of normal rotation speeds detected by the rotation speed detection unit 134 at the present time.

  If an abnormal pump condition has occurred in step 204, the determination is affirmed and the routine proceeds to step 206. If it is determined in step 204 that no abnormal pump condition has occurred, the determination is negative and the routine proceeds to step 208.

  In step 206, the control unit 124 causes the execution unit 122 to start executing the pump handling process, and then proceeds to step 206. The pump handling process is an example of one of a plurality of processes according to the present invention. An example of the pump handling process includes at least one of a pump abnormality notification process, a pump rotation speed adjustment process, and a pump stop process.

  Here, the pump abnormality notification process and the pump stop process are processes that contribute to the elimination of the pump abnormal state, and the pump rotational speed adjustment process is a fuel cell although a pump abnormal state has occurred. This process is required to continue power generation using the stack.

  The above-described pump abnormality notification process refers to, for example, a process in which the occurrence of a pump abnormal condition is notified by displaying information indicating that a pump abnormal condition has occurred on the display 108.

  Here, as one of the above pump abnormality notification processes, a visible display which is a display by the display 108 is illustrated, but the present invention is not limited to this. For example, it may be an audible display that outputs a sound indicating that an abnormal pump condition has occurred, or a permanent visual display in which information indicating that an abnormal pump condition has been recorded on paper or the like is output by a printer. May be. A plurality of visible display, audible display, and permanent visible display may be combined.

  The pump rotation speed adjustment process is based on, for example, correlation information 121 corresponding to the current combination of the current amount in the fuel cell stack, the combustion temperature, and the flow rate of the raw material gas among the plurality of correlation information 121. , Refers to a process in which the rotational speed of the pump 28 is adjusted. In other words, this refers to processing in which the rotation speed of the pump 28 is controlled so that the correlation between the combustion temperature and the fuel utilization rate at the present time matches the correlation between the combustion temperature and the fuel utilization rate indicated by the correlation information 121.

  The pump stop process refers to a process for stopping the operation of the pump 28, for example. The “stop” mentioned here naturally includes the meaning of complete stop of the operation of the pump 28, but also includes the stop of the meaning of suppressing the operation of the pump 28 to the extent that power generation by the fuel cell stack is not performed. When executing the pump rotation speed adjustment process, the pump stop process, etc., for example, the current value of the fuel cell stack and other basic raw material fluids may be changed as necessary.

  In addition, when the process which combined the said pump rotation speed adjustment process and said pump stop process is performed by the execution part 122, for example, after the said pump rotation speed adjustment process is performed, a pump abnormal state is eliminated. When there is not, the above-described pump stop process may be executed.

  In step 208, the control unit 124 determines whether or not the source gas system abnormality information indicating that the source gas system is in an abnormal state has occurred based on the first flow rate information acquired in the process of step 202. The source gas system refers to an element that directly or indirectly affects the normal supply of the source gas to the vaporizer 16. The elements that directly or indirectly affect the normal supply of the raw material gas to the vaporizer 16 include, for example, the flow sensor 64, the blower 30, the raw material gas pipe P1, and the blower 30 and the communication I / F 112. At least one of the electrical systems between the two.

  For example, in step 208, when the flow rate indicated by the first flow rate information acquired in the process of step 202 is not included in the second predetermined range, it is determined that the source gas system abnormality information has occurred. In Step 208, when the flow rate indicated by the first flow rate information acquired in the processing of Step 206 is included in the second predetermined range, it is determined that the source gas system abnormality information has not occurred.

  Here, the second predetermined range refers to a range determined in advance by a test using an actual machine, a computer simulation, or the like as a normal flow rate range detected by the flow rate sensor 64 at the present time.

  If a source gas system abnormal state has occurred in step 208, the determination is affirmed and the routine proceeds to step 210. If the source gas system abnormal state has not occurred in step 208, the determination is negative and the routine proceeds to step 212.

  In step 210, the control unit 124 causes the execution unit 122 to start executing the source gas system corresponding process, and then proceeds to step 212. In addition, the raw material gas system corresponding | compatible process is an example of one of the some processes which concern on this invention. As an example of the raw material gas system corresponding process, at least one of a raw material gas system abnormality notification process, a blower adjustment process, and a blower stop process may be mentioned.

  Here, the source gas system abnormality notification process and the blower stop process are processes that contribute to the elimination of the source gas system abnormal state, and the blower adjustment process has a source gas system abnormal state. However, this process is necessary for continuing the power generation by the fuel cell stack.

  The above-mentioned source gas system abnormality notification process refers to, for example, a process in which information indicating that a source gas system abnormality state has occurred is displayed on the display 108 to notify the occurrence of the source gas system abnormality state.

  In addition, although visible display is illustrated here as one of said raw material gas type | system | group abnormality notification processes similarly to said pump abnormality notification process, this invention is not limited to this. For example, it may be an audible display that outputs a voice that an abnormal state of the raw material gas system has occurred, or information that indicates that an abnormal state of the raw material gas system has occurred is recorded on a sheet or the like by a printer and output permanently. It may be visible. A plurality of visible display, audible display, and permanent visible display may be combined.

  The blower adjustment process is, for example, based on the correlation information 121 corresponding to the current combination of the current amount, the combustion temperature, and the flow rate of the oxidizing gas in the fuel cell stack among the plurality of correlation information 121. This refers to a process in which the amount of gas delivered by at least one of 30, 32 is adjusted. In other words, the blower adjustment process described above refers to the correlation between the combustion temperature and the fuel utilization rate indicated by the correlation information 121 with reference to the physical quantity related to the oxidizing gas, as the correlation between the current combustion temperature and the fuel utilization rate. Is a process in which the amount of gas delivered by at least one of the blowers 30 and 32 is adjusted so as to match the above. Here, the physical quantity related to the oxidizing gas refers to, for example, the “oxidizing gas utilization rate” in the following equation (5).

  (Oxidizing gas utilization rate) = (Amount of oxidizing gas used for reaction) / (Flow rate of oxidizing gas) (5)

  The blower stop process refers to, for example, a process for stopping the gas delivery by the blowers 30 and 32. Note that “stop” here includes the meaning of complete stoppage of gas delivery by the blowers 30 and 32, but the gas delivery by the blowers 30 and 32 is suppressed to such an extent that power generation by the fuel cell stack is not performed. This includes stopping in the sense of When performing the blower adjustment process, the blower stop process, and the like, for example, the current value of the fuel cell stack and other basic raw material fluids may be changed as necessary.

  In addition, when the process which combined the said blower adjustment process and said blower stop process is performed by the execution part 122, for example, after the said blower adjustment process was performed, the source gas system abnormal state was not eliminated In this case, the blower stop process may be executed.

  In step 212, the control unit 124 determines whether or not oxidizing gas system abnormality information indicating that the oxidizing gas system is in an abnormal state has occurred based on the second flow rate information acquired in the process of step 202. The oxidizing gas system refers to an element that directly or indirectly affects the normal supply of oxidizing gas to the permeation section 52. The elements that directly or indirectly affect the normal supply of the oxidizing gas to the transmission unit 52 include, for example, the oxidizing gas itself, the blower 32, the oxidizing gas pipe P5, and the blower 32 and the communication I / F 112. At least one of the electrical systems between the two.

  For example, in step 212, when the flow rate indicated by the second flow rate information acquired in the process of step 202 is not included in the third predetermined range, it is determined that the oxidizing gas system abnormality information has occurred. In step 212, when the flow rate indicated by the second flow rate information acquired in the process of step 202 is included in the third predetermined range, it is determined that no oxidizing gas system abnormality information has occurred.

  Here, the third predetermined range refers to a range determined in advance by a test using an actual machine, a computer simulation, or the like as a normal flow rate range detected by the flow sensor 66 at the present time.

  If an oxidizing gas system abnormal condition has occurred in step 212, the determination is affirmed and the routine proceeds to step 214. In step 212, if an oxidizing gas system abnormal state has not occurred, the determination is negative, and the routine proceeds to step 220 shown in FIG.

  In step 214, the control unit 124 causes the execution unit 122 to start execution of the oxidizing gas system corresponding process, and then proceeds to step 220. The oxidizing gas system handling process is an example of one of a plurality of processes according to the present invention. An example of the oxidizing gas system handling process includes at least one of an oxidizing gas system abnormality notification process, the blower adjustment process, and the blower stop process.

  Here, the oxidant gas system abnormality notification process and the blower stop process are processes that contribute to the elimination of the oxidant gas system abnormal state, and the blower adjustment process is performed while the oxidant gas system abnormal state occurs. This process is necessary for continuing the power generation by the fuel cell stack.

  The oxidizing gas system abnormality notification process refers to, for example, a process for notifying the occurrence of an oxidizing gas system abnormal condition by displaying information indicating that an oxidizing gas system abnormal condition has occurred on the display 108.

  Here, as one example of the oxidizing gas system abnormality notification process, a visible display is illustrated as in the pump abnormality notification process, but the present invention is not limited to this. For example, it may be an audible display that outputs a sound that an oxidative gas system abnormal state has occurred, or information that indicates that an oxidative gas system abnormal state has occurred is recorded on a sheet or the like by a printer and output permanently. It may be visible. A plurality of visible display, audible display, and permanent visible display may be combined.

  In addition, when the process which combined the said blower adjustment process and said blower stop process is performed by the execution part 122, for example, after performing said blower adjustment process, an oxidizing gas type abnormal state was not eliminated. In this case, the blower stop process may be executed.

  In step 220 shown in FIG. 6, the control unit 124 acquires non-supply system factor information, and then proceeds to step 222.

  Here, the non-supply system factor information refers to information indicating a factor used for specifying occurrence of a non-supply system abnormal state. In this step 218, voltage information, temperature information, pressure information, and gas leakage information are employed as an example of non-supply system factor information.

  In step 222, the control unit 124 determines whether or not a previous stack external leak has occurred based on the non-supply system factor information acquired in the process of step 220.

  The front stack external leak refers to an abnormal state in which gas may leak from the front fuel cell stack 22 to the outside. The possibility that gas is leaking from the front fuel cell stack 22 refers to the possibility that at least one of the oxidizing gas and the fuel gas is leaking. Here, the anode off gas leaking from the front stage fuel cell stack 22 means that the anode off gas leaks from a place other than the anode off gas pipes P6 and P6-2 in the front stage fuel cell stack 22.

  In step 222, when all of the first to sixth conditions are satisfied, it is determined that the previous stack external leak has occurred. Note that the determination may vary depending on the degree of external leakage, but here it is assumed that no significant external leakage has occurred.

  The first condition refers to a condition that the voltage indicated by the first voltage information is included in the fourth predetermined range. Here, the fourth predetermined range refers to a range determined in advance by a test using an actual machine, computer simulation, or the like as a normal voltage range detected by the voltage sensor 68 at the present time.

  The second condition refers to a condition that the voltage indicated by the second voltage information is not included in the fifth predetermined range. Here, the fifth predetermined range refers to a range determined in advance by a test using an actual machine, a computer simulation, or the like as a normal voltage range detected by the voltage sensor 70 at the present time.

  The third condition refers to a condition that the detection result by the gas leak sensor 87 indicated by the gas leak information matches the predetermined detection result. The predetermined detection result refers to a detection result indicating that no leaked gas is detected by the gas leak sensor 87.

  The fourth condition refers to a condition that the pressure indicated by the second pressure information is included in the sixth predetermined range. Here, the sixth predetermined range refers to a range determined in advance by an actual machine test, computer simulation, or the like as a range of pressure lower than the current normal pressure detected by the pressure sensor 58.

  The fifth condition refers to a condition that the pressure indicated by the third pressure information is not included in the seventh predetermined range. Here, the seventh predetermined range refers to a pressure determined in advance by a test using an actual machine, a computer simulation, or the like as a normal pressure range detected by the pressure sensor 60 at the present time. Note that the present invention is established even without the fifth condition.

  The sixth condition refers to a condition that the pressure indicated by the first pressure information is included in the eighth predetermined range and the pressure indicated by the fourth pressure information is included in the ninth predetermined range. Here, the eighth predetermined range refers to a range determined in advance by a test using an actual machine, a computer simulation, or the like as a pressure range lower than the current normal pressure detected by the pressure sensor 56. The ninth predetermined range refers to a range determined in advance by a test using an actual machine, a computer simulation, or the like as a pressure range lower than the current normal pressure detected by the pressure sensor 62.

  In step 222, if a front stack external leak has occurred, the determination is affirmed, and the routine proceeds to step 224. If it is determined in step 222 that the previous stack external leak has not occurred, the determination is negative and the routine proceeds to step 226.

  In step 224, the control unit 124 causes the execution unit 122 to start executing the front-stage external leak handling process that is a process contributing to the elimination of the front-stage stack external leak, and then proceeds to step 226. The pre-stage external leak handling process is an example of one of a plurality of processes according to the present invention. As an example of the pre-stage external leak handling process, there is at least one of the pre-stage external leak notification process, the blower adjustment process, and the blower stop process.

  Here, the front-stage external leak notification process and the blower stop process are processes that contribute to the elimination of the front-stage stack external leak, and the blower adjustment process is performed in the fuel cell stack although the front-stage stack external leak has occurred. This is the process required to continue the power generation.

  The front-stage external leak notification process refers to, for example, a process in which occurrence of a front-stage stack external leak is notified by displaying information indicating that a front-stage stack external leak has occurred on the display 108.

  Here, as one of the previous-stage external leak notification processes, a visible display is illustrated as in the pump abnormality notification process, but the present invention is not limited to this. For example, it may be an audible display that outputs a sound indicating that a previous stack external leak has occurred, or a permanent visual display in which information indicating that a previous stack external leak has occurred is recorded on a sheet of paper by a printer and output. It may be. A plurality of visible display, audible display, and permanent visible display may be combined.

  In addition, when the process which combined the said blower adjustment process and said blower stop process is performed by the execution part 122, for example, after the above-mentioned blower adjustment process is performed, the former stage stack external leak is not eliminated In addition, the blower stop process described above may be executed.

  In step 226, the control unit 124 determines whether or not a previous stack internal leak has occurred based on the non-supply system factor information acquired in step 220.

  Here, the front stack internal leak refers to, for example, an abnormal state in which the gas does not react at the anode or the cathode, and the gas may move as it is from one of the cathode 22A and the anode 22B to the other. .

  In step 226, when the first condition is not satisfied and the second and third conditions are satisfied, it is determined that the internal leakage in the previous stack has occurred.

  Note that the determination process in step 226 is not limited to the above example, and may be a determination process shown as the following first or second modification.

  The determination process according to the first modified example does not satisfy the first condition, satisfies the second and third conditions, and satisfies the fourth or sixth condition. In addition, it is a determination process in which it is determined that a previous stack internal leak has occurred.

  The determination process according to the second modified example is a determination process in which it is determined that a previous stack internal leak has occurred when the fourth or sixth condition is satisfied.

  If it is determined in step 226 that a previous stack internal leak has occurred, the determination is affirmed and the routine proceeds to step 228. If it is determined in step 226 that no internal leak has occurred in the previous stack, the determination is negative and the process proceeds to step 230.

  In step 228, the control unit 124 causes the execution unit 122 to start execution of the pre-stage internal leak handling process that is a process that contributes to the elimination of the pre-stage stack internal leak, and then proceeds to step 230. The upstream internal leak handling process is an example of one of a plurality of processes according to the present invention. As an example of the pre-stage internal leak handling process, there is at least one of the pre-stage internal leak notification process, the blower adjustment process, and the blower stop process.

  Here, the pre-stage internal leak notification process and the blower stop process are processes that contribute to the elimination of the pre-stack internal leak, and the blower adjustment process is performed in the fuel cell stack although the pre-stack internal leak occurs. This is the process required to continue the power generation.

  The front-stage internal leak notification process refers to, for example, a process in which occurrence of a front-stage stack internal leak is notified by displaying information indicating that a front-stage stack internal leak has occurred on the display 108.

  In addition, although visible display is illustrated here as one of the front stage internal leak alerting | reporting processes similarly to the pump abnormality alerting | reporting process, this invention is not limited to this. For example, it may be an audible display that outputs a sound indicating that a previous stack internal leak has occurred, or a permanent visual display in which information indicating that a previous stack internal leak has occurred is recorded on a sheet of paper by a printer and output. It may be. A plurality of visible display, audible display, and permanent visible display may be combined.

  In addition, when the process which combined the said blower adjustment process and said blower stop process is performed by the execution part 122, for example, after the above-mentioned blower adjustment process is performed, the case where the previous stack internal leak is not eliminated In addition, the blower stop process described above may be executed.

  In step 230, the control unit 124 determines whether or not a fuel regenerator gas leak has occurred based on the non-supply system factor information acquired in the process of step 220.

  The fuel regenerator gas leak refers to an abnormal state in which a specific gas may leak from the fuel regenerator 34. Here, the specific gas refers to, for example, the leakage gas described above.

  In step 230, it is determined that a fuel regenerator gas leak has occurred when the second condition is satisfied and the third condition is not satisfied.

  If the fuel regenerator gas leak has occurred in step 230, the determination is affirmed and the routine proceeds to step 232. If the fuel regenerator gas leak does not occur in step 230, the determination is negative and the routine proceeds to step 233A.

  In step 232, the control unit 124 causes the execution unit 122 to start execution of a gas leak handling process that is a process that contributes to the elimination of the fuel regenerator gas leak, and then proceeds to step 233A. The gas leakage handling process is an example of one of a plurality of processes according to the present invention. An example of the gas leak handling process includes at least one of a gas leak notification process, a bypass process, the blower adjustment process, and the blower stop process.

  Here, the gas leak notification process and the blower stop process are processes that contribute to the elimination of the fuel regenerator gas leak, and the bypass process and the blower adjustment process are performed while the fuel regenerator gas leak occurs. This is a process required to continue power generation by the fuel cell stack.

  The gas leak notification process refers to, for example, a process for notifying the occurrence of a fuel regenerator gas leak by displaying information indicating that a fuel regenerator gas leak has occurred on the display 108.

  In addition, although visible display is illustrated here as one of the gas leak countermeasure processes similarly to the pump abnormality notification process, the present invention is not limited to this. For example, it may be an audible display that outputs a sound indicating that a fuel regenerator gas leak has occurred, or information indicating that a fuel regenerator gas leak has occurred is recorded on a sheet or the like by a printer and output permanently. It may be visible. A plurality of visible display, audible display, and permanent visible display may be combined.

  Bypass processing refers to processing for shifting from the non-bypass mode to the bypass mode. The non-bypass mode refers to an operation mode in which the anode off-gas pipe P6 and the regenerated fuel gas pipe P8 are not bypassed, that is, an operation mode in which the solenoid valve 88 is closed and the solenoid valves 90 and 91 are opened. The bypass mode is an operation mode in which the anode off-gas pipe P6 and the regeneration fuel gas pipe P8 are bypassed via the bypass pipe 12P, that is, an operation mode in which the electromagnetic valve 88 is opened and the electromagnetic valves 90 and 91 are closed. Point to.

  In addition, when the process which combined at least 1 of said bypass process and said blower adjustment process and said blower stop process is performed by the execution part 122, for example, among bypass process and said blower adjustment process When the fuel regenerator gas leakage is not resolved even after at least one of the above is executed, the blower stop process described above may be executed.

  In step 233A, the control unit 124 determines whether or not a fuel regenerator internal leak has occurred based on the non-supply system factor information acquired in the process of step 220.

  The fuel regenerator internal leak refers to an abnormal state in which, for example, the sweep gas may leak from the permeation unit 52 to the inflow unit 50 via the separation membrane 92. In addition, it indicates an abnormal state in which the anode off gas may leak from the inflow part 50 to the permeation part 52 through the separation membrane 92.

  In step 233A, when the first to third conditions are satisfied, it is determined that a fuel regenerator internal leak has occurred.

  In this step 233A, the case where it is determined that the fuel regenerator internal leak has occurred when the above first to third conditions are satisfied is illustrated, but the present invention is not limited to this. . For example, when the above first to third conditions are satisfied and the fourth or sixth conditions are satisfied according to the specifications and installation environment of the fuel cell system main body 12, the fuel regenerator internal leak may occur. You may make it determine with having generate | occur | produced. Further, for example, when the above first to third conditions are satisfied and the above fifth condition is satisfied according to the specifications, installation environment, etc. of the fuel cell system main body 12, the fuel regenerator internal leak It may be determined that occurrence has occurred. Further, for example, when the above first to third conditions are satisfied and the fourth or sixth conditions are not satisfied, depending on the specifications and installation environment of the fuel cell system main body 12, the inside of the fuel regenerator It may be determined that a leak has occurred.

  In step 233A, if a fuel regenerator internal leak has occurred, the determination is affirmed and the routine proceeds to step 233B. If there is no fuel regenerator internal leak at step 233A, the determination is negative and the routine proceeds to step 234.

  In step 233B, the control unit 124 causes the execution unit 122 to start execution of the regenerator internal leak handling process, which is a process contributing to the elimination of the fuel regenerator internal leak, and then proceeds to step 234. The regenerator internal leak handling process is an example of one of a plurality of processes according to the present invention. An example of the regenerator internal leak handling process includes at least one of a regenerator internal leak notification process, the bypass process, the blower adjustment process, and the blower stop process.

  The regenerator internal leak notification process refers to, for example, a process in which information indicating that a fuel regenerator internal leak has occurred is displayed on the display 108 to notify the occurrence of a fuel regenerator internal leak.

  Here, as one of the regenerator internal leak countermeasure processing, a visible display is illustrated as in the pump abnormality notification processing, but the present invention is not limited to this. For example, it may be an audible display that outputs a sound indicating that a fuel regenerator internal leak has occurred, or information indicating that a fuel regenerator internal leak has occurred is recorded on a sheet or the like by a printer and output permanently. It may be visible. A plurality of visible display, audible display, and permanent visible display may be combined.

  In step 234, the control unit 124 determines whether or not the fuel regenerator deterioration has occurred based on the non-supply system factor information acquired in the process of step 220.

The fuel regenerator deterioration refers to an abnormal state in which the fuel regenerator 34 may be deteriorated at a predetermined level or more due to deterioration with time or corrosion. Here, it is assumed that the removal rate of CO ₂ and H ₂ O has decreased. The predetermined degree refers to, for example, a degree determined in advance by a test using a real machine, a computer simulation, or the like as a degree capable of realizing power generation efficiency within a range preset as a standard range of power generation efficiency. .

  In step 234, it is determined that the fuel regenerator deterioration has occurred when the first to fifth conditions are satisfied and the seventh condition is satisfied.

  Here, the seventh condition refers to a condition that the pressure indicated by the first pressure information is included in the tenth predetermined range and the pressure indicated by the fourth pressure information is included in the eleventh predetermined range. . Here, the tenth predetermined range refers to a range determined in advance by a test using an actual machine, a computer simulation, or the like as a range of pressure higher than the normal pressure detected by the pressure sensor 56 at the present time. The eleventh predetermined range refers to a range determined in advance by a test using an actual machine, computer simulation, or the like as a range of pressure higher than the normal pressure detected by the pressure sensor 62 at the present time.

  If the fuel regenerator deterioration has occurred in step 234, the determination is affirmed and the routine proceeds to step 236. If the fuel regenerator deterioration has not occurred in step 234, the determination is negative and the routine proceeds to step 238.

  In step 236, the control unit 124 causes the execution unit 122 to start executing the deterioration handling process that is a process that contributes to the elimination of the deterioration of the fuel regenerator, and then proceeds to step 238. The deterioration handling process is an example of one of a plurality of processes according to the present invention. An example of the deterioration handling process includes at least one of a fuel regenerator deterioration notification process, the bypass process, the blower adjustment process, and the blower stop process. Here, the fuel regenerator deterioration notifying process refers to, for example, a process of notifying the occurrence of the fuel regenerator deterioration by displaying on the display 108 information indicating that the fuel regenerator deterioration has occurred.

  The fuel regenerator deterioration notification process and the blower stop process are processes that contribute to the elimination of the fuel regenerator deterioration, and the bypass process and the blower adjustment process cause the fuel regenerator deterioration. However, this process is necessary for continuing the power generation by the fuel cell stack.

  Here, as the fuel regenerator deterioration notification process, a visible display is exemplified as in the above-described pump abnormality notification process, but the present invention is not limited to this. For example, it may be an audible display that outputs a sound indicating that the fuel regenerator has deteriorated, or a permanent visual display in which information indicating that the fuel regenerator has deteriorated is recorded on a sheet or the like by a printer and output. It may be. A plurality of visible display, audible display, and permanent visible display may be combined.

  In step 238, the control unit 124 determines whether or not a post-stack external leak has occurred based on the non-supply system factor information acquired in step 220.

  The rear stack external leakage refers to an abnormal state in which gas may leak from the rear fuel cell stack 24. The possibility of gas leaking from the rear fuel cell stack 24 refers to the possibility of leakage of at least one of the oxidizing gas and the regenerated fuel gas. Here, the used gas leaking from the rear fuel cell stack 24 means that the used gas is leaking from places other than the pipes P9 and P10 in the rear fuel cell stack 24.

  In step 238, if the second condition is not satisfied, it is determined that a rear stack external leak has occurred.

  In step 238, if a rear stack external leak has occurred, the determination is affirmative and the routine proceeds to step 240. If it is determined in step 238 that no post-stack external leak has occurred, the determination is negative and the routine proceeds to step 242.

  In step 240, the control unit 124 causes the execution unit 122 to start executing the rear-stage external leak handling process that is a process contributing to the elimination of the rear-stage stack external leak, and then proceeds to step 242. The post-stage external leak handling process is one example of a plurality of processes according to the present invention. As an example of the post-stage external leak countermeasure process, at least one of the post-stage external leak notification process, the blower adjustment process, and the blower stop process is given.

  Here, the post-stage external leak notification process and the blower stop process are processes that contribute to the elimination of the post-stack external leak, and the blower adjustment process is performed in the fuel cell stack although the post-stack external leak has occurred. This is the process required to continue the power generation.

  The post-stage external leak notification process refers to, for example, a process in which the occurrence of the post-stage stack external leak is notified by displaying information indicating that the post-stage stack external leak has occurred on the display 108.

  In addition, here, as one of the post-stage external leak notification processes, the visible display is illustrated as in the pump abnormality notification process, but the present invention is not limited to this. For example, it may be an audible display that outputs a sound indicating that a rear stack external leak has occurred, or a permanent visual display in which information indicating that a rear stack external leak has occurred is recorded on a sheet or the like by a printer and output. It may be. A plurality of visible display, audible display, and permanent visible display may be combined.

  In addition, when the execution unit 122 executes a process that combines the blower adjustment process and the blower stop process, for example, when the rear-stage stack external leak is not resolved even after the blower adjustment process is executed. In addition, the blower stop process described above may be executed.

  In step 242, the control unit 124 determines whether or not a rear stack internal leak has occurred based on the non-supply system factor information acquired in step 220.

  Here, the rear stack internal leak refers to, for example, an abnormal state in which the gas does not react at the anode or the cathode, and the gas may move as it is from one of the cathode 24A and the anode 24B to the other. .

  In step 242, it is determined that the rear stack internal leak has occurred when the first to third conditions are satisfied and the fourth or sixth condition is satisfied.

  In step 242, if a rear stack internal leak has occurred, the determination is affirmed, and step 244 is entered. If it is determined in step 243 that there is no rear stack internal leak, the determination is negative and the routine proceeds to step 246.

  In step 244, the control unit 124 causes the execution unit 122 to start execution of the rear-stage internal leak handling process that is a process contributing to the elimination of the rear-stage stack internal leak, and then proceeds to step 246. The post-stage internal leak handling process is an example of one of a plurality of processes according to the present invention. As an example of the rear stage internal leak handling process, at least one of the rear stage internal leak notification process, the blower adjustment process, the blower stop process, and the power generation stop process is given.

  Here, the rear-stage internal leak notification process, the blower stop process, and the power generation stop process are processes that contribute to the elimination of the rear-stage stack internal leak, and the blower adjustment process generates a rear-stage stack internal leak. However, this process is necessary for continuing the power generation by the fuel cell stack.

  The post-stage internal leak notification process refers to, for example, a process in which the occurrence of the post-stage stack internal leak is notified by displaying information indicating that the post-stage stack internal leak has occurred on the display 108.

  Here, as one of the subsequent internal leak notification processes, a visible display is illustrated as in the pump abnormality notification process, but the present invention is not limited to this. For example, it may be an audible display that outputs a sound indicating that a rear stack internal leak has occurred, or a permanent visual display in which information indicating that a rear stack internal leak has occurred is recorded on paper or the like by a printer. It may be. A plurality of visible display, audible display, and permanent visible display may be combined.

  The power generation stop process refers to a process for stopping power generation in the post-stage fuel cell stack 24. In this case, for example, a post-stage fuel cell is provided by providing a switch (not shown) in an external circuit that is a movement path of electrons generated in the anode 24B from the anode 24B to the cathode 24A, and turning off the switch to disconnect the external circuit. Power generation in the stack 24 is stopped.

  In addition, when the execution unit 122 executes a process that combines the blower adjustment process and the blower stop process, for example, when the internal leak of the rear stack is not resolved after the blower adjustment process is executed. In addition, the blower stop process described above may be executed.

  In step 246, the control unit 124 determines whether or not an end condition that is a condition for ending the maintenance process is satisfied. The end condition indicates, for example, a condition that the receiving device 104 has received an instruction to end the maintenance process.

  If the end condition is not satisfied at step 246, the determination is negative and the routine proceeds to step 200 shown in FIG. If it is determined in step 246 that the end condition is satisfied, the determination is affirmed and the maintenance process ends.

  As described above, in the fuel cell system 10, priority is given to an abnormal state having a larger influence on the fuel cell system main body 12 among a plurality of abnormal states based on the detection result by the detection unit 113. Then, the execution unit 122 is controlled so that the corresponding processing is executed. Therefore, according to the fuel cell system 10, it is possible to preferentially deal with an abnormal state having a large influence degree among a plurality of abnormal states occurring in the fuel cell system main body 12.

  Further, in the fuel cell system 10, a plurality of abnormal states in the fuel cell system main body 12 are roughly divided into supply system abnormal states and non-supply system abnormal states, and influences on the fuel cell system main body 12. The degree is higher in the supply system abnormal state than in the non-supply system abnormal state. Therefore, according to the fuel cell system 10, the supply system abnormal condition can be prioritized (preceded) over the non-supply system abnormal condition.

  In the fuel cell system 10, the supply system maintenance process is executed when the detection result by the detection unit 113 is a detection result indicating the occurrence of a supply system abnormal state. Further, when the detection result by the detection unit 113 is not the detection result indicating the occurrence of the supply system abnormal state and the detection result by the detection unit 113 is the detection result indicating the occurrence of the non-supply system abnormal state, the non-supply system maintenance is performed. Processing is executed. Therefore, according to the fuel cell system 10, the supply system maintenance process can be executed with priority over the non-supply system maintenance process.

  Further, in the fuel cell system 10, the blower stop process described above is executed. Therefore, according to the fuel cell system 10, it is possible to suppress the seriousness of the abnormal state of the supply system as compared with the case where the gas delivery by the blowers 30 and 32 is continued.

  In the fuel cell system 10, the above-described blower adjustment process is executed by the execution unit 122 when an abnormal state occurs in the fuel cell system main body 12. Therefore, according to the fuel cell system 10, even when an abnormal state occurs in the fuel cell system main body 12, power generation by the fuel cell stack can be continued.

  In the above embodiment, since the control gas is common to the oxidizing gas and the sweep gas, it is not determined whether or not an abnormal state of the sweep gas, which is an abnormal state of the sweep gas, has occurred. When the gas is a system of another system, the control unit 124 may determine whether or not an abnormal sweep gas state has occurred. In this case, for example, at the end of the supply system maintenance process, a sweep gas abnormal condition determination process for determining whether or not a sweep gas abnormal condition has occurred, and a sweep gas handling process that is a process corresponding to the sweep gas abnormal condition are executed. You can do so.

  In the sweep gas abnormal state determination process, for example, when the fifth condition is satisfied and the eighth condition is satisfied, it is determined that the sweep gas abnormal state has occurred. Here, the eighth condition refers to a condition that the temperature indicated by the sixth temperature information is outside the twelfth predetermined range. Here, the twelfth predetermined range refers to a range determined in advance by an actual machine test, computer simulation, or the like as the normal temperature range detected by the temperature sensor 82 at the present time.

  The sweep gas handling process is an example of one of a plurality of processes according to the present invention. An example of the sweep gas handling process includes a sweep gas abnormality notification process, the blower adjustment process, or the blower stop process. Other examples of the sweep gas handling process include a process combining the sweep gas abnormality notification process and the blower adjustment process, or a process combining the sweep gas abnormality notification process and the blower stop process.

  The sweep gas abnormality notification process refers to, for example, a process in which the occurrence of a sweep gas abnormality state is notified by displaying information indicating that a sweep gas abnormality state has occurred on the display 108.

  Here, as one of the sweep gas abnormality notification processes, a visible display is illustrated as in the pump abnormality notification process, but the present invention is not limited to this. For example, it may be an audible display that outputs a sound that an abnormal state of sweep gas has occurred, or a permanent visual display in which information indicating that an abnormal state of sweep gas has occurred is recorded and output by a printer. It may be. A plurality of visible display, audible display, and permanent visible display may be combined.

  In the above embodiment, in the supply system maintenance process shown in FIG. 5, the source gas system corresponding process is executed before the oxidizing gas system corresponding process, and the pump corresponding process is performed earlier than the source gas system corresponding process. Although implemented, the present invention is not limited to this. For example, if the magnitude relationship of the degree of influence affecting the fuel cell system main body 12 is “pump abnormal state <source gas system abnormal state <oxidizing gas system abnormal state”, the priority relationship to be executed is , “Pump-compatible treatment <source gas-based treatment <oxidizing gas-based treatment”. Thus, in the supply system maintenance process, according to the specifications of the fuel system main body 12 and the installation environment, etc., corresponding to the magnitude relationship of the degree of influence that the abnormal state has on the fuel cell system main body 12, What is necessary is just to define the priority of the response | compatibility process which should be performed.

  Note that, in the non-supply system maintenance process shown in FIG. 6, as in the supply system maintenance process shown in FIG. That is, in the non-supply system maintenance process shown in FIG. 6, the subsequent external leak response process is executed earlier than the subsequent internal leak response process. In addition, the deterioration handling process is executed before the subsequent external leak handling process. In addition, the gas leakage handling process is executed before the degradation handling process. In addition, the pre-stage internal leak handling process is executed before the gas leak handling process. Furthermore, the pre-stage external leak handling process is executed before the pre-stage internal leak handling process. In the non-supply system maintenance process shown in FIG. 6 as well, in the same way as the supply system maintenance process shown in FIG. 5, the fuel cell system main body 12 is in an abnormal state depending on the specifications and installation environment of the fuel system main body 12. The priority of the corresponding process to be executed may be determined in accordance with the magnitude relationship of the influence level affected by.

  Moreover, although the case where generation | occurrence | production of abnormal condition etc. was alert | reported by the visual display using the display 108 was illustrated in the said embodiment, this invention is not limited to this. For example, information indicating the occurrence of an abnormal state or the like is transmitted from the fuel cell system 10 to a communication device such as a smart device or a server that can communicate with the fuel cell system 10, and the communication device generates an abnormal state or the like. This notification may be realized. Also in this case, at least one of a visible display by a display mounted on the communication apparatus, an audible display by a speaker mounted on the communication apparatus, and a permanent visible display by a printer connected to the communication apparatus is performed. do it. In addition, when a vibrator is mounted on the communication device, the occurrence of an abnormal state or the like may be notified by vibrating the vibrator.

  When the fuel cell system 10 is remotely operated from a remote management center, information indicating the occurrence of an abnormal state or the like is transmitted from the fuel cell system 10 to a host computer or the like of the management center, and the host computer or the like generates an abnormal state or the like. This notification may be realized.

  Moreover, although the case where the maintenance program 120 is read from the secondary storage unit 118 is illustrated in the above embodiment, it is not necessarily stored in the secondary storage unit 118 from the beginning. For example, as shown in FIG. 7, the maintenance program 120 may be first stored in an arbitrary portable storage medium 300 such as an SSD, a USB memory, or a CD-ROM. In this case, the maintenance program 120 of the storage medium 300 is installed in the fuel cell system 10, and the installed maintenance program 120 is executed by the CPU 114.

  Also, the maintenance program 120 is stored in a storage unit such as another computer or server device connected to the fuel cell system 10 via a communication network (not shown), and the maintenance program 120 responds to the request of the fuel cell system 10. It may be downloaded in response. In this case, the downloaded maintenance program 120 is executed by the CPU 114.

  The maintenance process described in the above embodiment is merely an example. Therefore, it goes without saying that unnecessary steps may be deleted, new steps may be added, and the processing order may be changed within a range not departing from the spirit.

  Moreover, although the execution part 122 and the control part 124 were illustrated by the software configuration using a computer in the said embodiment, this invention is not limited to this. For example, instead of a software configuration using a computer, a function corresponding to the execution unit 122 and a function corresponding to the control unit 124 only by a hardware configuration such as a field-programmable gate array (FPGA) or an application specific integrated circuit (ASIC). May be realized. Further, the function corresponding to the execution unit 122 and the function corresponding to the control unit 124 may be realized by a combination of a software configuration and a hardware configuration.

  In the above-described embodiment, the fuel cell system main body 12 including the two-stage fuel cell stack including the front-stage fuel cell stack 22 and the rear-stage fuel cell stack 24 is illustrated, but the present invention is not limited to this. . For example, the present invention can be applied to a fuel cell system main body including a single-stage fuel cell stack. Moreover, it is not limited to the two-stage type, and may be increased to three stages, four stages, and the like. In addition, the number of stacks per stage may be plural. Further, the present invention can be established without the fuel regenerator 34. Further, the present invention can be realized without the air cooling device 36 and the tank 26. Further, the reforming may be performed directly by the fuel cell without using the reformer 18.

  Moreover, in the said embodiment, although the fuel cell system main-body part 12 containing two fuel cell stacks was illustrated, this invention is not limited to this. As an example, as shown in FIG. 8, the present invention can be realized even if three fuel cell stacks are used in a two-stage system.

  As an example, as shown in FIG. 8, the fuel cell stack 400 is different from the fuel cell stack 10 shown in FIG. 1 in that it has a fuel cell system main body 402 instead of the fuel cell system main body 12. The fuel cell system main body 402 is different from the fuel cell system main body 12 in that the first fuel cell stack 21 is replaced with the first fuel cell stack 22 instead of the front fuel cell stack 22. Further, the fuel cell system main body 402 is different from the fuel cell system main body 12 in that it includes a front-stage second fuel cell stack 404, a voltage sensor 406, and a temperature sensor 408.

  The basic configuration of the front-stage first fuel cell stack 21 is the same as that of the front-stage fuel cell stack 22. The basic configuration of the front stage second fuel cell stack 404 is the same as that of the front stage first fuel cell stack 21, and the front stage second fuel cell stack 404 corresponds to the cathode 404A corresponding to the cathode 22A and the anode 22B. And an anode 404B.

  The voltage sensor 406 is provided between the cathode 404A and the anode 404B, and detects the voltage at the cathode 404A and the anode 404B.

  The temperature sensor 408 is provided in the front second fuel cell stack 404 and detects the temperature in the front second fuel cell stack 404.

  The fuel gas pipe P4 branches to the fuel gas pipe P4-1 at the branch portion B1, and the fuel gas is supplied to the anode 404B via the fuel gas pipe P4-1. The oxidizing gas pipe P5 branches to the oxidizing gas pipe P5-1 at the branch portion B2. One end of the oxidizing gas pipe P5-1 is connected to the oxidizing gas pipe P5 at the branch B2, and the other end of the oxidizing gas pipe P5-1 is connected to the cathode 404A. An oxidizing gas is supplied from the oxidizing gas pipe P5 to the cathode 404A through the oxidizing gas pipe P5-1. Therefore, in the front stage second fuel cell stack 404, power is generated in each fuel cell by the same reaction as that in the front stage first fuel cell stack 21, and each fuel cell generates heat during power generation.

  One end of a cathode offgas pipe P14 through which the cathode offgas flows is connected to the cathode 404A, and the cathode offgas is discharged from the cathode 404A to the cathode offgas pipe P14. Further, the cathode offgas pipe P13 merges with the cathode offgas pipe P14 at the junction I2. That is, the other end of the cathode offgas pipe P13 is connected to the cathode offgas pipe P14 at the junction I2. The other end of the cathode offgas pipe P14 is connected to the cathode 24A. Accordingly, the cathode offgas discharged from the cathode 22A to the cathode offgas pipe P13 and the cathode offgas discharged from the cathode 404A to the cathode offgas pipe P14 are supplied to the cathode 24A.

  One end of an anode offgas pipe P6-2 that is a pipe through which the anode offgas flows is connected to the anode 404B, and the anode offgas is discharged from the anode 404B to the anode offgas pipe P6-2. The anode off gas pipe P6-2 merges with the anode off gas pipe P6 at the junction I1.

  A portion of the anode off-gas pipe P6 on the downstream side of the joining portion I1 is connected to the inflow portion 50 via the fourth heat exchanging portion 44 and the first heat exchanging portion 38.

  The anode off gas discharged from the anodes 22B and 404B flows into the inflow portion 50, and the fuel regenerator 34 separates carbon dioxide and water vapor from the anode off gas flowing into the inflow portion 50.

  The permeable part exhaust gas sent from the permeable part 52 is supplied to the cathode 22A as an oxidizing gas containing oxygen through the oxidizing gas pipe P5, and is supplied to the cathode 404A through the oxidizing gas pipes P5 and P5-1.

  In the example shown in FIG. 8, the anode off-gas of the first-stage first fuel cell stack 21 and the first-stage second fuel cell stack 404 is supplied only to the fuel regenerator 34, but the present invention is not limited to this. It is not something. For example, the present invention is also applied to a fuel cell system main body including a circulating fuel cell stack that supplies an anode off gas to at least one of the anodes 22B and 404B together with the fuel gas delivered from the reformer 18. Is possible.

  All documents, patent applications and technical standards mentioned in this specification are to the same extent as if each individual document, patent application and technical standard were specifically and individually stated to be incorporated by reference. Incorporated by reference in the book.

DESCRIPTION OF SYMBOLS 10 Fuel cell system 12 Fuel cell system main-body part 20 Combustor 22 The front | former stage fuel cell stack 24 The back | latter stage fuel cell stack 113 Detection part 120 Maintenance program 122 Execution part 124 Control part

Claims (7)

A plurality of abnormal states occurring in a fuel cell system main body having a fuel cell stack, each corresponding to each of a plurality of abnormal states classified according to the degree of influence affecting the fuel cell system main body. An execution unit that executes the process of
Based on the detection result by the detection unit capable of detecting a plurality of factors each capable of specifying the occurrence of each of the plurality of abnormal states, priority is given to the abnormal state having the larger influence degree among the plurality of abnormal states. A control unit that controls the execution unit so that a corresponding process of the plurality of processes is executed;
A maintenance device for a fuel cell system.   The plurality of abnormal states are a supply system abnormal state that is an abnormal state related to a supply system that supplies fluid to be supplied to the power generation of the fuel cell stack to a supplied part included in the fuel cell system main body, and the supply system abnormal state 2. The maintenance device for a fuel cell system according to claim 1, further comprising: a non-supply system abnormal state that is an abnormal state different from a non-supply system abnormal state having a smaller influence than the supply system abnormal state.   When the detection result by the detection unit is a detection result indicating the occurrence of the supply system abnormal state, the control unit performs processing corresponding to the supply system abnormal state, and the detection result by the detection unit is The execution unit is configured to execute processing corresponding to the non-supply system abnormal state in the case of a detection result indicating the occurrence of the non-supply system abnormal state instead of the detection result indicating the occurrence of the supply system abnormal state. The maintenance device for a fuel cell system according to claim 2, wherein the maintenance device is controlled.   The maintenance apparatus for a fuel cell system according to claim 3, wherein the process corresponding to the supply system abnormal state is a process including a process of stopping the operation of the supply system. The fuel cell system body includes a combustor that burns combustible gas,
At least one of the plurality of processes includes a fuel utilization rate calculated based on a combustion temperature that is a temperature in the combustor, a flow rate of a raw material gas, and a current amount in the fuel cell stack, and the combustion The predetermined correlation with the temperature includes a process of operating the fuel cell system main body so as to match the correlation between the fuel utilization rate and the combustion temperature at the present time with reference to a physical quantity related to the oxidizing gas. The maintenance device for a fuel cell system according to any one of claims 1 to 4, wherein the maintenance device is a process. A maintenance device for a fuel cell system according to any one of claims 1 to 5,
A fuel cell system body having a fuel cell stack,
The execution unit included in the maintenance device for the fuel cell system is classified into a plurality of abnormal states that occur in the fuel cell system main body, and has an influence on the fuel cell system main body. A fuel cell system that executes a plurality of processes respectively corresponding to a plurality of abnormal states. Computer
The program for functioning as the said execution part and the said control part which are contained in the maintenance apparatus for fuel cell systems of any one of Claims 1-5.