JP5282881B2 - Fuel cell system - Google Patents

Description

  The present invention relates to a fuel cell system.

Patent Document 1 below discloses a technique related to a fuel cell vehicle equipped with a fuel cell system, in which surplus regenerative power generated during regeneration by a drive motor is consumed by an air compressor. And in the technique of this patent document 1, in order to prevent the dry up which may arise with the oxidizing gas supplied to a fuel cell from an air compressor, a fuel cell is made to generate electric power and the moisture content in a fuel cell is raised.
JP 2007-157586 A

  By the way, when shifting from high load operation, which is an operation state when the required power generation amount from the drive motor is high, to low load operation, which is an operation state when the required power generation amount is low, it takes time to change the temperature of the cooling water. Therefore, the operation is shifted to the low load operation while the temperature of the cooling water is high. During low-load operation, the amount of power generation is small and the amount of generated water is also small. Therefore, if the temperature of the cooling water is high during low-load operation, the degree of dryness in the fuel cell will progress and there is a risk of dry-up. In Patent Document 1, the fuel cell is caused to generate electric power in order to ensure a wet state in the fuel cell. At the same time, the compressor is also driven to consume surplus power, so that the fuel cell is supplied from the compressor. The generated water is taken out by the oxidizing gas, and the inside of the fuel cell may be dried.

  The present invention has been made to solve the above-described problems caused by the prior art, and an object thereof is to provide a fuel cell system capable of preventing the fuel cell from being dried.

  In order to solve the above-described problems, a fuel cell system according to the present invention includes a fuel cell that receives supply of a reaction gas and generates electric power through an electrochemical reaction of the reaction gas, and the oxidizing gas of the reaction gas. An oxidant gas supply channel for supplying the fuel cell, a compressor provided in the oxidant gas supply channel, for supplying the oxidant gas to the fuel cell, and an oxidant off-gas exhausted from the fuel cell are discharged. An oxidizing off-gas discharge passage for the gas, a back pressure valve provided in the oxidizing off-gas discharge passage for adjusting the pressure of the oxidizing gas in the fuel cell, and at least the compressor in the oxidizing gas supply passage A shut-off valve provided on either the downstream side or the oxidizing off-gas discharge flow path for shutting off or allowing the supply of the oxidizing gas to the fuel cell; A cooling water circulation mechanism that circulates cooling water to the fuel cell, and the cooling water temperature is higher than a predetermined temperature, and the required power generation amount from the power consuming device that consumes the power of the fuel cell is less than the predetermined power generation amount And a shutoff valve control means for closing the shutoff valve.

  According to this invention, when the temperature of the cooling water is higher than the predetermined temperature and the required power generation amount from the power consuming device is less than the predetermined power generation amount, the shutoff valve that cuts off or allows the supply of the oxidizing gas to the fuel cell. Therefore, it is possible to prevent water from being taken out of the fuel cell.

  The fuel cell system may further include power generation stop control means for stopping power generation of the fuel cell when the cutoff valve is closed by the cutoff valve control means.

  As a result, in addition to shutting off the supply of the oxidizing gas to the fuel cell by closing the shut-off valve, the supply of the oxidizing gas from the compressor can be stopped. It becomes possible to suppress.

  In the fuel cell system, a livestock unit capable of charging the electric power of the fuel cell, and before the shutoff valve is closed by the shutoff valve control means, the remaining capacity of the power storage unit charges the power storage unit. Charge control means for causing the fuel cell to generate power and charging the power storage unit until the remaining capacity is equal to or greater than the predetermined capacity when the remaining capacity is less than the predetermined capacity set for limiting; Can be provided.

  As a result, when the remaining capacity of the power storage unit is small, the shutoff valve can be closed after charging the power storage unit, so the power of the power storage unit is supplied to the power consuming device while the shutoff valve is closed. It is possible to continue operation while supplying.

  In the fuel cell system, the shut-off valve control means, when the value obtained by subtracting the amount of water taken out of the fuel cell from the amount of water generated by the power generation of the fuel cell is greater than a predetermined value, The shutoff valve can be prevented from closing.

  As a result, when the water content in the fuel cell is high and the possibility of dry-up is low, the operation can be continued with the shutoff valve open.

  In the fuel cell system, a bypass channel that branches from a downstream side of the compressor of the oxidizing gas supply channel, bypasses the fuel cell, and joins the oxidizing off-gas discharge channel, and is provided in the bypass channel. An adjustment valve for adjusting the flow rate of the oxidizing gas that joins the oxidizing gas supply flow path from the oxidizing gas supply flow path, and the adjustment when the shut-off valve is closed by the shut-off valve control means. Adjusting valve control means for opening a valve, wherein the shut-off valve is at least downstream of the branch point to the bypass flow path in the oxidizing gas supply flow path or the oxidizing off gas discharge flow path It can provide in any one of the upstream from the confluence | merging point with the said bypass flow path.

  Thus, even if the oxidizing gas is supplied from the compressor after the shut-off valve is closed, the oxidizing gas supplied from the compressor can be discharged to the oxidizing off-gas discharge channel through the bypass channel.

  According to the present invention, drying in the fuel cell can be prevented.

  DESCRIPTION OF EXEMPLARY EMBODIMENTS Hereinafter, preferred embodiments of a fuel cell system according to the invention will be described with reference to the accompanying drawings. In the embodiment, a case will be described in which the fuel cell system according to the present invention is used as an on-vehicle power generation system of a fuel cell vehicle (FCHV).

  First, with reference to FIG. 1, the structure of the fuel cell system in embodiment is demonstrated. FIG. 1 is a configuration diagram schematically illustrating a fuel cell system according to an embodiment.

  As shown in the figure, a fuel cell system 1 includes a fuel cell 2 that generates electric power by an electrochemical reaction upon receiving supply of an oxidizing gas and a fuel gas as reaction gases, and air as an oxidizing gas to the fuel cell 2. An oxidizing gas piping system 3 to be supplied; a hydrogen gas piping system 4 for supplying hydrogen as fuel gas to the fuel cell 2; a cooling system 5 (cooling water circulation mechanism) for circulating and supplying cooling water to the fuel cell 2; It has a power system 6 that charges and discharges power, and a control unit 7 (shut-off valve control means, power generation stop control means, charge control means, adjustment valve control means) that controls the entire system.

  The fuel cell 2 is, for example, a polymer electrolyte fuel cell, and has a stack structure in which a large number of single cells are stacked. The single cell has a cathode electrode (air electrode) on one surface of an electrolyte made of an ion exchange membrane, an anode electrode (fuel electrode) on the other surface, and further sandwiches the cathode electrode and anode electrode from both sides. It has the structure which has a pair of separator. In this case, hydrogen gas is supplied to the hydrogen gas flow path of one separator, oxidizing gas is supplied to the oxidizing gas flow path of the other separator, and electric power is generated by the chemical reaction of these reaction gases. The fuel cell 2 is provided with a voltage sensor V that detects the output voltage of the fuel cell and a current sensor A that detects the output current of the fuel cell.

  The oxidizing gas piping system 3 compresses the air taken in through the filter, sends out the compressed air as the oxidizing gas, an oxidizing gas supply flow path 32 for supplying the oxidizing gas to the fuel cell 2, The oxidizing off-gas discharge flow path 33 for discharging the oxidizing off-gas discharged from the fuel cell 2 and a part of the oxidizing gas discharged from the compressor 31 join the oxidizing off-gas discharge flow path 33 by bypassing the fuel cell 2. And a bypass flow path 34 for the purpose.

  On the outlet side of the compressor 31, a flow rate sensor F that measures the flow rate of the oxidizing gas discharged from the compressor 31 is provided. The fuel cell 2 is disposed downstream of the branch point to the bypass channel 34 in the oxidizing gas supply channel 32 and upstream of the junction point with the bypass channel 34 in the oxidizing off-gas discharge channel 33. There are provided shut-off valves 35 and 36 for shutting off or allowing the supply of the oxidizing gas. A back pressure valve 37 for adjusting the pressure of the oxidizing gas in the fuel cell 2 is provided upstream of the shutoff valve 36 in the oxidizing off gas discharge flow path 33. A pressure sensor P for detecting the pressure of the oxidizing gas in the fuel cell 2 is provided on the outlet side of the fuel cell 2 in the oxidizing off gas discharge channel 33.

  The bypass channel 34 is a channel that branches from the downstream side of the compressor 31 in the oxidizing gas supply channel 32, bypasses the fuel cell 2, and joins the oxidizing off gas discharge channel 33. The bypass channel 34 is provided with an adjustment valve 38 that adjusts the flow rate of the oxidizing gas that is merged from the oxidizing gas supply channel 32 to the oxidizing off-gas discharge channel 33. The adjustment valve 38 is electrically connected to the control unit 7, and the opening degree of the adjustment valve 38 is controlled by the control unit 7.

  The hydrogen gas piping system 4 includes a hydrogen tank 40 as a fuel supply source storing high-pressure hydrogen gas, and a hydrogen gas supply flow as a fuel gas supply channel for supplying the hydrogen gas in the hydrogen tank 40 to the fuel cell 2. A passage 41 and a hydrogen circulation passage 42 as a fuel circulation passage for returning the hydrogen off-gas discharged from the fuel cell 2 to the hydrogen gas supply passage 41 are provided. The hydrogen gas supply channel 41 is provided with a regulator 43 that adjusts the pressure of the hydrogen gas to a preset secondary pressure. The hydrogen circulation channel 42 is provided with a hydrogen pump 44 that pressurizes the hydrogen off-gas in the hydrogen circulation channel 42 and sends it to the hydrogen gas supply channel 41 side.

  The cooling system 5 includes a radiator 51 that cools the cooling water, a cooling water circulation passage 52 that circulates and supplies the cooling water to the fuel cell 2 and the radiator 51, and a cooling water circulation pump 53 that circulates the cooling water to the cooling water circulation passage 52. Have The radiator 51 is provided with a radiator fan 54. A temperature sensor T that detects the temperature of the cooling water is provided on the outlet side of the fuel cell 2 in the cooling water circulation passage 52. The position where the temperature sensor T is provided may be on the inlet side of the fuel cell 2.

  The power system 6 includes a DC / DC converter 61, a battery 62 (power storage unit) as a secondary battery, a traction inverter 63, a traction motor 64 as a power consuming device, and various auxiliary inverters (not shown). Have. The DC / DC converter 61 is a direct-current voltage converter that adjusts the direct-current voltage input from the battery 62 and outputs it to the traction inverter 63 side, and the direct-current voltage input from the fuel cell 2 or the traction motor 64. And adjusting the output to the battery 62. By such a function of the DC / DC converter 61, charging / discharging of the battery 62 is realized.

  The battery 62 is configured such that battery cells are stacked and a constant high voltage is used as a terminal voltage, and surplus power can be charged or power can be supplementarily supplied under the control of a battery computer (not shown). The battery 62 is provided with an SOC sensor S for detecting the remaining capacity (State of Charge) of the battery 62. The traction inverter 63 converts a direct current into a three-phase alternating current and supplies it to the traction motor 64. The traction motor 64 is, for example, a three-phase AC motor, and constitutes a main power source of a fuel cell vehicle on which the fuel cell system 1 is mounted. The auxiliary inverter is an electric motor control unit that controls driving of each motor, converts a direct current into a three-phase alternating current, and supplies the three-phase alternating current to each motor.

  The control unit 7 measures an operation amount of an acceleration operation member (for example, an accelerator) provided in the fuel cell vehicle, and controls an acceleration request value (for example, a required power generation amount from a power consuming device such as the traction motor 64). Receives information and controls the operation of various devices in the system. In addition to the traction motor 64, the power consuming device includes, for example, auxiliary equipment required for operating the fuel cell 2 (for example, the motor of the compressor 31, the hydrogen pump 44, the cooling water circulation pump 53, etc.), the vehicle This includes actuators used in various devices (transmissions, wheel control devices, steering devices, suspension devices, etc.) involved in traveling, air conditioning devices (air conditioners) for passenger spaces, lighting, audio, and the like.

  The control unit 7 physically includes, for example, a CPU, a memory 71, and an input / output interface. The memory 71 includes, for example, a ROM that stores control programs and control data processed by the CPU, and a RAM that is mainly used as various work areas for control processing. These elements are connected to each other via a bus. Various sensors such as a temperature sensor T, a flow sensor F, and an SOC sensor S are connected to the input / output interface, and various drivers for driving the compressor 31, the shutoff valves 35 and 36, the adjustment valve 38, and the like are connected. Has been.

  The CPU receives various measurement results from various sensors via the input / output interface according to a control program stored in the ROM, and executes various control processes by processing using various data in the RAM. Further, the CPU controls the entire fuel cell system 1 by outputting control signals to various drivers via the input / output interface. Below, the control process performed by the control part 7 of this embodiment is demonstrated.

  When the predetermined condition is satisfied, the control unit 7 stops the power generation of the fuel cell 2 and performs dry-up prevention control for closing the shut-off valves 35 and 36, thereby reducing the cooling water temperature to lower the cooling water temperature. Control (described later) is executed. The predetermined conditions include the following conditions.

  The first condition is that the temperature of the cooling water measured by the temperature sensor T is higher than a predetermined temperature. The predetermined temperature is, for example, the temperature of cooling water set in advance for each operation state of the fuel cell 2, and corresponds to the upper limit temperature of the optimum water temperature range in each operation state. The operating state of the fuel cell 2 can be set in advance in a plurality of stages according to the required power generation amount from the power consuming device such as the traction motor 64. For example, depending on the required power generation amount from the power consuming device, the high-load operation in which the required power generation amount is higher than the predetermined first power generation amount, the low-load operation in which the required power generation amount is lower than the predetermined second power generation amount, the required power generation A distinction can be made between medium load operation in which the amount falls between a predetermined first power generation amount and a predetermined second power generation amount.

  The second condition corresponds to the flow rate of the oxidizing gas measured by the flow sensor F being less than a predetermined flow rate. As the predetermined flow rate, for example, the pressure of the oxidant gas in the fuel cell 2 is within a range of the oxidant gas flow rate that can raise the pressure of the oxidant gas in the fuel cell 2 to a pressure that can maintain the water balance indicating the state of water in and out. The lower limit flow rate applies. Therefore, when the flow rate of the oxidizing gas is less than the predetermined flow rate, the current oxidizing gas flow rate is necessary to maintain the pressure of the oxidizing gas in the fuel cell 2 and the water balance in the fuel cell 2 positively. It shows that it is not possible to raise it to the correct pressure.

  Here, the water balance in the fuel cell 2 can be calculated by subtracting the amount of water brought out as water vapor by the oxidizing gas supplied to the fuel cell 2 from the amount of water generated by the power generation of the fuel cell 2. it can. The amount of moisture taken out can be calculated from the humidity and gas amount of the gas at the cathode outlet of the fuel cell 2. Since the humidity of the gas can be calculated based on the temperature of the cooling water and the amount of power generation, a humidity map for calculating the humidity of the gas from the temperature of the cooling water and the amount of power generation is obtained in advance by experiments, etc. It is good also as storing in the memory 71 of the control part 7 at the time of manufacture shipment.

  By monitoring the trend of the water balance in the fuel cell, when the water balance in the fuel cell 2 is decreasing, it is understood that the water content in the fuel cell is reduced and drying can proceed. When the water balance is increased, it becomes possible to grasp that the moisture content in the fuel cell is increased and the wetness can proceed.

  Since the flow rate of the oxidizing gas is determined based on the required power generation amount from the power consuming device that consumes the power of the fuel cell 2, the second condition is that the required power generation amount from the power consuming device is the predetermined power generation amount. It can be replaced by being less than the amount.

  The third condition corresponds to the water balance in the fuel cell 2 being a predetermined value or less. As the predetermined value, for example, 0 or a value slightly larger than 0 can be set. By setting a value slightly larger than 0, for example, when the water balance continues to decrease within a positive range, it is possible to execute dry-up prevention control before it falls negative.

  By adding this third condition to the above-mentioned predetermined condition, execution of dry-up prevention control is prohibited when the possibility of dry-up is low, such as when moving from high-load operation to low-load operation temporarily. It becomes possible to make it. Here, when the dry-up prevention control is executed, the power generation of the fuel cell 2 is stopped, and the shutoff valves 35 and 36 are closed. Therefore, if the dry-up prevention control is executed until the vehicle is temporarily moved to the low load operation, the response is delayed when the fuel cell 2 is started or when the shut-off valves 35 and 36 are opened when the high load operation is resumed. Can occur. Therefore, in a situation where the vehicle is temporarily moved to a low-load operation and it is assumed that the possibility of dry-up is low, the start-up of the fuel cell 2 is suppressed by suppressing the execution of the dry-up prevention control. In addition, it is possible to reduce the opportunity for response delay due to the opening operation of the shutoff valves 35 and 36 as much as possible.

  The fourth condition corresponds to the remaining capacity of the battery 62 measured by the SOC sensor S being greater than or equal to a predetermined capacity. As the predetermined capacity, for example, a capacity set to limit charging of the battery 62 is applicable. Therefore, charging is restricted when the remaining capacity of the battery 62 is greater than or equal to a predetermined capacity, and charging is permitted when the remaining capacity of the battery 62 is less than the predetermined capacity.

  When the remaining capacity of the battery 62 is less than the predetermined capacity, the control unit 7 executes power generation amount increase control for increasing the power generation amount, and performs water content increase control for increasing the water content in the fuel cell 2. . The power generation amount increase control corresponds to, for example, control in which the power generation amount of the fuel cell 2 is increased more than the required power generation amount from the power consuming device to generate surplus power, and the surplus power is charged in the battery 62.

  Examples of the water content increase control include control for reducing the stoichiometric ratio of the oxidizing gas and control for increasing the pressure of the oxidizing gas in the fuel cell 2. Since the stoichiometric ratio of the oxidizing gas is represented by a surplus ratio of the amount of oxidizing gas supplied to the fuel cell 2 with respect to the amount of oxidizing gas consumed in the fuel cell 2, control for reducing the stoichiometric ratio of the oxidizing gas is performed by the oxidizing gas. The control can be replaced with a control for reducing the supply amount of.

  By adding this fourth condition to the predetermined condition, when the remaining capacity of the battery 62 is small, the battery 62 can be executed after the battery 62 is charged. It is possible to keep the 62 running as long as possible.

  The dry-up prevention control may be executed when all of the above four conditions are satisfied, but it is not always necessary to satisfy all the conditions. For example, when both the first condition and the second condition are satisfied, it can be assumed that the water temperature is high by shifting from the high load operation to the low load operation. The dry-up prevention control may be executed when the condition is satisfied.

  The control unit 7 corresponds to, for example, control for increasing the rotation speed of the motor of the cooling water circulation pump 53 and control for increasing the rotation speed of the radiator fan 54 as the cooling water temperature lowering control described above.

  Next, control processing executed in the fuel cell system of the present embodiment will be described using the flowchart shown in FIG. This control process is started, for example, when the ignition key is turned on, and is repeatedly executed until the operation ends.

  First, the control unit 7 determines whether or not the temperature of the cooling water measured by the temperature sensor T is higher than a predetermined temperature (step S101). If this determination is NO (step S101; NO), this control process ends.

  On the other hand, when it is determined in step S101 that the temperature of the cooling water is higher than the predetermined temperature (step S101; YES), the control unit 7 determines that the flow rate of the oxidizing gas measured by the flow sensor F is predetermined. It is determined whether it is less than the flow rate (step S102). If this determination is NO (step S102; NO), this control process is terminated.

  On the other hand, when it is determined in step S102 that the flow rate of the oxidizing gas is less than the predetermined flow rate (step S102; YES), the control unit 7 determines whether the water balance in the fuel cell is equal to or less than the predetermined value. It is determined whether or not (step S103). If this determination is NO (step S103; NO), this control process is terminated.

  On the other hand, when it is determined in step S103 that the water balance in the fuel cell is equal to or less than the predetermined value (step S103; YES), the control unit 7 determines that the remaining battery 62 measured by the SOC sensor S remains. It is determined whether or not the capacity is equal to or greater than a predetermined capacity (step S104). When this determination is NO (step S104; NO), the control unit 7 executes power generation amount increase control for increasing the power generation amount of the fuel cell 2 beyond the required power generation amount and charging the battery 62 with surplus power. (Step S105).

  Subsequently, the control unit 7 performs water content increase control for increasing the water content in the fuel cell 2 (step S106). Subsequently, the control unit 7 executes cooling water temperature lowering control for reducing the temperature of the cooling water (step S109), and ends this control process.

  On the other hand, when it is determined in step S104 that the remaining capacity of the battery 62 is equal to or larger than the predetermined capacity (step S104; YES), the control unit 7 stops the power generation of the fuel cell (step S107). The shut-off valves 35 and 36 are closed (step S108). Subsequently, the control unit 7 executes cooling water temperature lowering control for reducing the temperature of the cooling water (step S109), and ends this control process.

  As described above, according to the fuel cell system 1 of the present embodiment, when the temperature of the cooling water is higher than the predetermined temperature and the required power generation amount from the power consuming device is less than the predetermined power generation amount, the fuel cell 2 Since the shutoff valves 35 and 36 for shutting off or allowing the supply of the oxidizing gas to the engine can be closed and the supply of the oxidizing gas from the compressor 31 can be stopped, it is possible to suppress the water from being taken out of the fuel cell 2. Can do.

  In the above-described embodiment, the shut-off valves 35 and 36 are provided at two locations, but it is not always necessary to provide them at two locations, and may be provided only at one of them.

  In the above-described embodiment, the power generation of the fuel cell 2 is stopped in the dry-up prevention control, but it is not always necessary to stop the fuel cell. If the power generation of the fuel cell 2 is continued by the dry-up prevention control, the oxidizing gas is supplied from the compressor 31. In this case, for example, the opening of the regulating valve 38 is adjusted to adjust the compressor. The oxidizing gas supplied from 31 may be discharged to the oxidizing off-gas discharge channel 33 via the bypass channel 34. Further, when the power generation of the fuel cell 2 is stopped by the dry-up prevention control, the adjustment valve 38 may be further opened. Thereby, the possibility that the oxidizing gas flows into the fuel cell 2 can be further reduced.

  Moreover, although the humidifier for humidifying the oxidizing gas supplied to the fuel cell 2 is not provided in the fuel cell system 1 in the above-described embodiment, a humidifier may be further provided. Specifically, the oxidizing gas supply flow path 32 and the oxidizing off gas discharge flow path 33 may be provided with a humidifier that humidifies the oxidizing gas pumped from the compressor 31 using the oxidizing off gas discharged from the fuel cell 2. Good.

  In the above-described embodiment, the case where the fuel cell system according to the present invention is mounted on a fuel cell vehicle has been described. However, the present invention is also applied to various mobile bodies (robots, ships, aircrafts, etc.) other than the fuel cell vehicle. The fuel cell system according to the invention can be applied. Moreover, the fuel cell system according to the present invention can also be applied to a stationary power generation system used as a power generation facility for buildings (houses, buildings, etc.).

It is a lineblock diagram showing typically the fuel cell system in an embodiment. It is a flowchart for demonstrating the control processing at the time of regeneration in embodiment.

Explanation of symbols

  DESCRIPTION OF SYMBOLS 1 ... Fuel cell system, 2 ... Fuel cell, 3 ... Oxidation gas piping system, 4 ... Hydrogen gas piping system, 5 ... Cooling system, 6 ... Electric power system, 7 ... Control part, 31 ... Compressor, 32 ... Oxidation gas supply flow , 33 ... Oxidized off gas discharge channel, 34 ... Bypass channel, 35, 36 ... Shut-off valve, 37 ... Back pressure valve, 38 ... Regulating valve, 51 ... Radiator, 52 ... Cooling water circulation channel, 53 ... Cooling water circulation pump, 54 ... Radiator fan, 61 ... DC / DC converter, 62 ... Battery, 63 ... Traction inverter, 64 ... Traction motor, 71 ... Memory, F ... Flow rate sensor, S ... SOC sensor, T ... Temperature sensor.

Claims (5)

A fuel cell that receives supply of a reactive gas and generates electric power by an electrochemical reaction of the reactive gas;
An oxidizing gas supply channel for supplying the oxidizing gas of the reaction gas to the fuel cell;
A compressor that is provided in the oxidizing gas supply flow path and supplies the oxidizing gas to the fuel cell;
An oxidation off-gas discharge flow path for discharging the oxidation off-gas discharged from the fuel cell;
A back pressure valve provided in the oxidizing off-gas discharge flow path for adjusting the pressure of the oxidizing gas in the fuel cell;
A shutoff valve provided at least on either the downstream side of the compressor in the oxidizing gas supply flow path or on the oxidizing offgas discharge flow path and shuts off or allows the supply of the oxidizing gas to the fuel cell; ,
A cooling water circulation mechanism that circulates and supplies cooling water to the fuel cell;
The temperature of the cooling water is higher than the preset upper limit temperature of the optimum water temperature range, and the required power generation amount from the power consuming device that consumes the power of the fuel cell indicates the state of water entering and exiting the fuel cell. Shut-off valve control means for closing the shut-off valve when the amount of power generation is less than that required to maintain the water balance positively ;
A fuel cell system comprising:   2. The fuel cell system according to claim 1, further comprising power generation stop control means for stopping power generation of the fuel cell when the cutoff valve is closed by the cutoff valve control means. A charge reservoir portion can be charged with electric power of the fuel cell,
Prior to closing the shut-off valve by the shut-off valve control means, when the remaining capacity of the power storage unit is less than a predetermined capacity set to limit charging of the power storage unit, the remaining capacity is 3. The fuel cell system according to claim 1, further comprising: charge control means for causing the fuel cell to generate power until a predetermined capacity or more is reached and charging the power storage unit with the generated power. Wherein said cutoff valve control means, the amount of water produced by power generation of the fuel cell, when the fuel cell outer water content by remote often brought in is characterized in that not closed the shut-off valve Item 4. The fuel cell system according to any one of Items 1 to 3. A bypass flow path that branches from the downstream side of the compressor of the oxidizing gas supply flow path, bypasses the fuel cell, and joins the oxidizing off gas discharge flow path;
An adjustment valve for adjusting a flow rate of the oxidizing gas provided in the bypass flow path and joined from the oxidizing gas supply flow path to the oxidizing off-gas discharge flow path;
Adjusting valve control means for opening the adjusting valve when the shut-off valve is closed by the shut-off valve control means; and
The shut-off valve is at least downstream from a branch point to the bypass flow channel in the oxidizing gas supply flow channel or upstream from a junction point with the bypass flow channel in the oxidation off-gas discharge flow channel. It is provided in any one of these, The fuel cell system of any one of Claims 1-4 characterized by the above-mentioned.

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