JP5734635B2 - Control method of fuel cell stack - Google Patents

Description

The present invention includes a fuel cell in which an electrolyte membrane / electrode structure provided with electrodes on both sides of an electrolyte membrane and a separator are stacked with a seal member interposed therebetween, and a fuel in which a plurality of the fuel cells are stacked control on the control method of the fuel cell stack.

  For example, in a polymer electrolyte fuel cell, an electrolyte membrane / electrode structure (MEA) in which an anode side electrode and a cathode side electrode are disposed on both sides of an electrolyte membrane made of a polymer ion exchange membrane is sandwiched by separators. Unit cell. This type of fuel cell is usually used as an in-vehicle fuel cell stack or the like by stacking a predetermined number of unit cells.

  In this type of fuel cell stack, it is necessary to grasp the internal state of the fuel cell, for example, temperature distribution, current density distribution or water distribution, in order to obtain a desired power generation performance and to exhibit a desired sealing function. . In particular, the water content of the MEA inside the fuel cell tends to affect the power generation performance and durability, and it is desired to accurately grasp the water content even during operation and stop of the fuel cell.

  Thus, for example, a fuel cell system disclosed in Patent Document 1 is known. This fuel cell system includes a fuel cell stack in which a plurality of membrane electrode assemblies that generate electricity by an electrochemical reaction between a fuel gas and an oxidant gas are stacked via a conductive separator, and the stack is fastened from both sides. Operating means for operating the fuel cell stack by supplying the fuel gas and oxidant gas to the fuel cell stack, and in-plane load distribution in the membrane electrode assembly during the operation by the operating means A load distribution estimating means for estimating the load, a load applying means for dividing the surface of the membrane electrode assembly into a plurality of regions and individually applying a load to each region, and a load distribution obtained by the load distribution estimating means Distribution bias reducing means for controlling the load applying means based on the above to reduce the in-plane load distribution bias in the membrane electrode assembly.

  The load distribution estimating means is a parameter detecting means for detecting an operating parameter which is at least one of a required current of the fuel cell stack, a temperature of the fuel cell stack, a supply pressure of the fuel gas, and a supply pressure of the oxidant gas. It has. Thereby, the load distribution in the surface of the membrane electrode assembly can be made uniform regardless of the operating state of the fuel cell.

  Further, the fuel cell system disclosed in Patent Document 2 has a membrane-electrode assembly in which both surfaces of an electrolyte membrane are sandwiched between a pair of catalyst layers, and receives the reaction gas to react with the electrochemical reaction of the reaction gas. A fuel cell that generates electric power, a first impedance corresponding to a resistance of the electrolyte membrane in a first frequency region, and a lower frequency region than the first frequency region. Using an impedance calculator that calculates a second impedance that is an impedance of the fuel cell in a second frequency region, and a differential impedance that is a difference between the second impedance and the first impedance, Water content calculating means for calculating the water content of the fuel cell. Thereby, it is supposed that the degree of dryness in the fuel cell can be grasped more accurately.

JP 2008-305686 A JP 2010-165463 A

  However, the above Patent Document 1 and Patent Document 2 have problems that special sensors are required and the apparatus becomes large and complicated. Moreover, there is a problem that measurement cannot always be performed in real time.

The present invention solves this type of problem, and it is possible to accurately estimate the membrane water content by a simple process, and furthermore, the operation control of the fuel cell can be satisfactorily performed based on the membrane water content. an object of the present invention is to provide a control method of the fuel cell stack.

In the present invention, an electrolyte membrane / electrode structure provided with electrodes on both sides of an electrolyte membrane and a separator are stacked with a seal member interposed therebetween, and power is generated with supplied fuel gas and oxidant gas, and The present invention relates to a method for controlling a fuel cell stack including a fuel cell cooled by a supplied cooling medium and in which a plurality of the fuel cells are stacked.

In this control method, when changing the load current of the fuel cell, corresponding to the actually measured clamping load, applied load applied to the seal member in the stacking direction, working pressure load and film of the stacking direction based on operating pressure Storing a relationship of loads in a table; measuring a tightening load applied to a plurality of the fuel cells in a stacking direction; and using the table to determine the membrane load based on the measured tightening load. a step Ru determined, before a step of calculating the water content of the electrolyte membrane from Kimaku load, based on the temperature of said calculated water content and the cooling medium, fuel gas and oxidant gas flow rate, of the cooling medium A step of adjusting at least one of the flow rate and the power generation amount.

  Furthermore, in this control method, the fuel cell stack is provided with a pair of end plates at both ends in the stacking direction of the plurality of fuel cells, and the pair of end plates are fixed integrally while maintaining a distance from each other. In addition, it is preferable that a load measuring mechanism for providing a plurality of load sensors is disposed between the pair of end plates.

  According to the present invention, the water content of the electrolyte membrane is calculated from the variation in the tightening load applied to the plurality of fuel cells in the stacking direction, so that the fuel cell stack state, for example, whether in operation or stopped It becomes possible to accurately and reliably estimate the water content of the electrolyte membrane.

  Thus, the water content of the membrane can be accurately estimated by a simple process, and the electrolyte membrane / electrode structure can be maintained in an efficient state. Therefore, it is possible to improve the power generation performance and suppress the deterioration of durability, and the fuel cell operation control can be satisfactorily performed based on the membrane water content.

It is a schematic illustration of a fuel cell stack for performing the engagement Ru control method embodiment of the present invention. FIG. 3 is an exploded perspective view of a main part of the fuel cell stack. It is a principal part disassembled perspective explanatory drawing of the fuel cell which comprises the said fuel cell stack. FIG. 4 is a cross-sectional view of the fuel cell taken along line IV-IV in FIG. 3. It is a relationship explanatory drawing of cell thickness and film | membrane load characteristic. It is a relationship explanatory drawing of membrane water content and swelling amount. It is explanatory drawing of the relationship between a film | membrane load and a film | membrane water content. It is explanatory drawing of the relationship between a working pressure load and the variation | change_quantity of a fastening load. It is an explanatory view of the relationship between the tightening load and the shared load. It is explanatory drawing for calculating a film | membrane load from a fastening load. 4 is a flowchart illustrating the control method during operation of the fuel cell stack. 4 is a flowchart illustrating the control method when the fuel cell stack is stopped.

As shown in FIG. 1, the fuel cell stack 10 for carrying out the engagement Ru control method embodiment of the present invention is incorporated into a vehicle-mounted fuel cell system 12. The fuel cell system 12 supplies a hydrogen supply device 14 for supplying hydrogen gas (hydrogen-containing gas) as a fuel gas and air (oxygen-containing gas) as an oxidant gas to the fuel cell stack 10. The air supply device 16, the cooling medium supply device 18 for supplying the cooling medium, the ECU (control device) 20 that performs overall control, and the fuel cell stack 10 are charged and power is supplied to the load A possible power storage device, for example, a battery 21 is provided.

  The fuel cell stack 10 includes a stacked body 24 in which a plurality of fuel cells 22 are stacked in the direction of arrow A (vertical direction). A first terminal plate 25a, a first insulating plate 26a, and a first end plate 28a are stacked on the lower end (one end) of the stacked body 24 in the stacking direction.

  As shown in FIGS. 1 and 2, the second terminal plate 25 b, the second insulating plate 26 b, the load measuring mechanism 30, and the second end plate 28 b are stacked on the upper end (the other end) of the stacked body 24 in the stacking direction. . A pressure mechanism 32 is provided on the second end plate 28b. The stacked body 24 may be configured by stacking a plurality of fuel cells 22 in the horizontal direction (arrow B direction or arrow C direction).

  As shown in FIGS. 3 and 4, in the fuel cell 22, the electrolyte membrane / electrode structure 34 is sandwiched between the first separator 36 and the second separator 38. The first separator 36 and the second separator 38 are made of, for example, a metal separator such as a steel plate, a stainless steel plate, an aluminum plate, or a plated steel plate, a carbon separator, or the like.

  As shown in FIG. 3, oxidation is performed at one end edge of the fuel cell 22 in the arrow B direction (horizontal direction) to supply air, which is an oxidant gas, in communication with each other in the arrow A direction that is the stacking direction. The agent gas inlet communication holes 40a and the fuel gas inlet communication holes 42a for supplying hydrogen gas as the fuel gas are arranged in the arrow C direction (horizontal direction).

  The other end edge of the fuel cell 22 in the direction of arrow B communicates with each other in the direction of arrow A, a fuel gas outlet communication hole 42b for discharging fuel gas, and an oxidant gas for discharging oxidant gas. The outlet communication holes 40b are arranged in the arrow C direction.

  A cooling medium inlet communication hole 44a for supplying a cooling medium and a cooling medium outlet communication hole 44b for discharging the cooling medium are provided at both ends of the fuel cell 22 in the direction of arrow C.

  An oxidant gas flow path 46 communicating with the oxidant gas inlet communication hole 40a and the oxidant gas outlet communication hole 40b is provided on the surface 36a of the first separator 36 facing the electrolyte membrane / electrode structure 34.

  A fuel gas passage 48 communicating with the fuel gas inlet communication hole 42a and the fuel gas outlet communication hole 42b is provided on the surface 38a of the second separator 38 facing the electrolyte membrane / electrode structure 34.

  A cooling medium that connects the cooling medium inlet communication hole 44a and the cooling medium outlet communication hole 44b between the surface 36b of the first separator 36 and the surface 38b of the second separator 38 that constitute the fuel cells 22 adjacent to each other. A flow path 50 is provided.

  The first seal member 52 is integrally or individually provided on the surfaces 36 a and 36 b of the first separator 36, and the second seal member 54 is integrally formed on the surfaces 38 a and 38 b of the second separator 38. Or it is provided separately.

  The first seal member 52 and the second seal member 54 are, for example, EPDM, NBR, fluororubber, silicon rubber, fluorosilicone rubber, butyl rubber, natural rubber, styrene rubber, chloroplane, or acrylic rubber, or a cushioning material. Or use packing material.

  The electrolyte membrane / electrode structure 34 includes, for example, a solid polymer electrolyte membrane 56 in which a perfluorosulfonic acid thin film is impregnated with water, and a cathode side electrode 58 and an anode side electrode 60 that sandwich the solid polymer electrolyte membrane 56. With.

  The cathode side electrode 58 and the anode side electrode 60 are formed by uniformly coating the surface of the gas diffusion layer with a gas diffusion layer made of carbon paper or the like and a porous carbon particle having a platinum alloy supported on the surface. An electrode catalyst layer. The electrode catalyst layers are formed on both surfaces of the solid polymer electrolyte membrane 56.

  As shown in FIG. 1, for example, a plurality of connecting bars 61 are bridged between a first end plate 28a and a second end plate 28b made of aluminum, and the first end plate 28a and the second end plate are spanned. The distance between 28b is kept constant. The connecting bars 61 have, for example, a long plate shape made of aluminum, and two connecting bars 61 are provided on the long side of the fuel cell stack 10 and one on the short side of the fuel cell stack 10. Is done. The connecting bar 61 is fixed to the side portions of the first end plate 28 a and the second end plate 28 b via screws 62.

  The first end plate 28a includes an oxidant gas inlet communication hole 40a, a fuel gas inlet communication hole 42a, a cooling medium inlet communication hole 44a, an oxidant gas outlet communication hole 40b, a fuel gas outlet communication hole 42b, and a cooling medium outlet communication hole. A manifold (not shown) that communicates with 44b and extends to the outside is provided, while the second end plate 28b is configured in a flat plate shape from which these and the seal member are omitted.

  As shown in FIG. 2, the load measuring mechanism 30 includes a pressure plate 64 placed on the second insulating plate 26b. The pressure plate 64 has, for example, rectangular recesses 66 formed in the vicinity of four corners. The The load measuring mechanism 30 includes a frame-shaped connecting member 68 and a load sensor, for example, a load cell 72, which is fixed to the four corners of the connecting member 68 via nuts 70.

  The connecting member 68 is provided with a spherical recess 74 having a spherical bottom surface in the vicinity of each load cell 72. Each load cell 72 is provided with a pressing member 76, and the pressing member 76 is disposed in each concave portion 66 of the pressing plate 64.

  The pressurizing mechanism 32 includes a plurality of, for example, four load adjustment bolts 78. Each load adjustment bolt 78 is screwed into a screw hole 79 formed in the second end plate 28 b, and each spherical tip 78 a is disposed in each spherical recess 74 of the connecting member 68. The center of each load adjustment bolt 78 and the center of each load cell 72 are displaced from each other.

  As shown in FIG. 1, the hydrogen supply device 14 includes a hydrogen tank 80 that stores high-pressure hydrogen, and the hydrogen tank 80 is disposed in a hydrogen supply path 82. The hydrogen supply path 82 communicates with the fuel gas inlet communication hole 42 a of the fuel cell stack 10 and is provided with a pressure reducing valve 84 and an ejector 86.

  The hydrogen supply device 14 includes a hydrogen circulation path (circulation pipe) 88 that communicates with the fuel gas outlet communication hole 42 b of the fuel cell stack 10, and the hydrogen circulation path 88 is provided with an ejector 86 with a gas-liquid separator 90 interposed therebetween. Communicate with. The ejector 86 is disposed in the piping part 88 a that constitutes the hydrogen circulation path 88.

  A drain pipe 88b is connected to the lower part of the gas-liquid separator 90, and a drain valve 92 is disposed in the drain pipe 88b. An exhaust pipe section 88c is connected to the pipe section 88a, and a diluter 96 is connected to the exhaust pipe section 88c through an on-off valve 94.

  The air supply device 16 includes an air pump 98. The air supply path 100 to which the air pump 98 is connected communicates with the oxidant gas inlet communication hole 40 a of the fuel cell stack 10 via the humidifier 102.

  The air supply device 16 has an air discharge path 104 that communicates with the oxidant gas outlet communication hole 40 b of the fuel cell stack 10. The air discharge path 104 extends outside the vehicle via the humidifier 102, and the dilution pipe 104a branches off. The dilution pipe 104 a is connected to the diluter 96 through the on-off valve 106. The humidifier 102 humidifies the new air by exchanging water between the used humidified air discharged to the air discharge path 104 and new air introduced to the air supply path 100. .

  The cooling medium supply device 18 includes a radiator 108. A cooling medium circulation path 110 is connected to the radiator 108, and both ends of the cooling medium circulation path 110 are connected to the cooling medium inlet communication hole 44 a and the cooling medium outlet communication hole 44 b of the fuel cell stack 10. A refrigerant pump 112 is interposed in the cooling medium circulation path 110.

  The hydrogen supply device 14, the air supply device 16, and the cooling medium supply device 18 are provided with sensors 114a, 114b, and 114c for detecting predetermined states, respectively. For example, the sensor 114a detects the flow rate, humidity or temperature of the fuel gas, the sensor 114b detects the flow rate or humidity of the oxidant gas, and the sensor 114c detects the temperature or flow rate of the cooling medium. A signal is sent to the ECU 20. The ECU 20 receives a load signal from a load cell 72 that is a load sensor, and detects a tightening load in the stacking direction of the entire fuel cell stack 10.

  The operation of the fuel cell stack 10 configured as described above will be described below.

  First, as shown in FIG. 1, in the air supply device 16, under the driving action of the air pump 98, the compressed air led out to the air supply path 100 is humidified by the humidifier 102 and then oxidized in the fuel cell stack 10. It is supplied to the agent gas inlet communication hole 40a.

  In the hydrogen supply device 14, the high-pressure hydrogen stored in the hydrogen tank 80 is depressurized via the pressure reducing valve 84 and sent to the hydrogen supply path 82. The fuel gas (hydrogen gas) is ejected from the ejector 86, and used fuel gas to be described later is sucked and supplied to the fuel gas inlet communication hole 42 a of the fuel cell stack 10.

  On the other hand, in the cooling medium supply device 18, under the action of the refrigerant pump 112, a cooling medium such as pure water, ethylene glycol, or oil is supplied from the cooling medium circulation path 110 to the cooling medium inlet communication hole 44 a of the fuel cell stack 10. .

  Therefore, as shown in FIG. 3, the oxidant gas is introduced into the oxidant gas flow path 46 of the first separator 36 from the oxidant gas inlet communication hole 40a. The oxidant gas is supplied to the cathode side electrode 58 constituting the electrolyte membrane / electrode structure 34 while moving in the arrow B direction.

  On the other hand, the fuel gas is introduced into the fuel gas passage 48 of the second separator 38 from the fuel gas inlet communication hole 42a. The fuel gas is supplied to the anode side electrode 60 constituting the electrolyte membrane / electrode structure 34 while moving in the arrow B direction.

  Therefore, in the electrolyte membrane / electrode structure 34, the oxidant gas supplied to the cathode side electrode 58 and the fuel gas supplied to the anode side electrode 60 are consumed by an electrochemical reaction in the electrode catalyst layer, thereby generating power. Is done.

  Next, the oxidant gas consumed by being supplied to the cathode-side electrode 58 is discharged in the direction of arrow A along the oxidant gas outlet communication hole 40b. On the other hand, the fuel gas consumed by being supplied to the anode electrode 60 is discharged in the direction of arrow A along the fuel gas outlet communication hole 42b.

  The cooling medium supplied to the cooling medium inlet communication hole 44 a is introduced into the cooling medium flow path 50 between the first separator 36 and the second separator 38 and then flows in the direction of arrow C. The cooling medium is discharged from the cooling medium outlet communication hole 44b after the electrolyte membrane / electrode structure 34 is cooled.

  As shown in FIG. 1, the oxidant gas is discharged from the oxidant gas outlet communication hole 40 b to the air discharge path 104. This oxidant gas is humidified with a new oxidant gas by the humidifier 102 and then discharged outside the vehicle, and is supplied to the diluter 96 through the dilution pipe 104a as necessary.

  On the other hand, the fuel gas is discharged from the fuel gas outlet communication hole 42 b to the hydrogen circulation path 88. After the fuel gas is introduced into the gas-liquid separator 90 and the water is separated and removed, the fuel gas is sucked into the ejector 86 from the pipe portion 88a. Therefore, the fuel gas is mixed with new fuel gas, introduced into the hydrogen supply path 82, and supplied to the fuel cell stack 10 as fuel gas. When the hydrogen purge is performed, the on-off valve 94 is opened and the fuel gas is introduced into the diluter 96.

  In addition, the cooling medium is returned to the cooling medium circulation path 110 from the cooling medium outlet communication hole 44 b and is cooled by the radiator 108 and then circulated and supplied to the fuel cell stack 10.

Next, a control method according to the present embodiment will be described below.

  First, the tightening load W (ALL) of the fuel cell stack 10 that is actually operated is actually measured, and the membrane load W (MEA) acting on the electrolyte membrane / electrode structure 34 is calculated from the tightening load W (ALL). The

  Specifically, the fuel cell stack 10 includes an operating pressure load W (OP) in the stacking direction based on the operating pressure, and a load load applied to the first seal member 52 and the second seal member 54 in the stacking direction. W (SEAL) occurs. Therefore, a relational expression of tightening load W (ALL) = operating pressure load W (OP) + load load W (SEAL) + membrane load W (MEA) is obtained.

  The electrolyte membrane / electrode structure 34 (particularly, the solid polymer electrolyte membrane 56) varies in water content depending on the operating state of the fuel cell stack 10, and the thickness dimension changes due to swelling. At that time, the electrolyte membrane / electrode structure 34 is constrained in the stacking direction by the first separator 36 and the second separator 38, and as shown in FIG. 5, the membrane load W along the cell thickness-membrane load characteristics. (MEA) changes.

  Here, the cell thickness means a thickness in a state where the electrolyte membrane / electrode structure 34 is sandwiched between the first separator 36 and the second separator 38. Further, the relationship between the load applied to the solid polymer electrolyte membrane 56 and the thickness of the solid polymer electrolyte membrane 56 is very close to the relationship between the load applied to the electrolyte membrane / electrode structure 34 and the cell thickness. On the other hand, in the gas diffusion layer and the electrode catalyst layer, the change in thickness based on the water content is very small with respect to the load applied to each.

  When the membrane load W (MEA) is changed from the first membrane load W1 (MEA) to the second membrane load W2 (MEA), the cell thickness change required for this load change is t μm. Then, in order for the cell thickness of the electrolyte membrane / electrode structure 34 having a humidity (water content) n1% to change by t μm, as shown in FIG. 6, the humidity (water content) change is (n2−n1)%. Is required. Therefore, the membrane load W (MEA) of the electrolyte membrane / electrode structure 34 and the water content of the electrolyte membrane / electrode structure 34 (particularly, the solid polymer electrolyte membrane 56) have the relationship shown in FIG.

  On the other hand, the total of the operating pressure load W (OP) and the variation amount of the tightening load W (ALL) have the relationship shown in FIG. Furthermore, the shared load between the load load W (SEAL) and the membrane load W (MEA) in the tightening load W (ALL) has the relationship shown in FIG. Since the inclination (variation amount) of the membrane load W (MEA) is large, it can be measured with high sensitivity.

  Thus, when the load current of the fuel cell 22 is changed, the relationship between the operating pressure load W (OP), the load load W (SEAL), and the membrane load W (MEA) corresponding to the actually measured tightening load W (ALL). Is shown in FIG. This is stored in the memory of the ECU 20 as a table.

  Therefore, as shown in FIG. 11, during operation of the fuel cell stack 10, the tightening load W (ALL) applied in the stacking direction of the fuel cell stack 10 is a plurality of load cells 72 constituting the load measuring mechanism 30. Is detected (actually measured) (step S1). Specifically, the tightening load W (ALL) is detected by adding the measured loads of the four load cells 72 together. The ECU 20 calculates the membrane load W (MEA) of the electrolyte membrane / electrode structure 34 from the detected tightening load W (ALL) (step S2).

Et al is based on the film weight W (MEA), membrane water content of the membrane electrode assembly 34 is calculated (step S3).

  In this case, in the present embodiment, the membrane load W (MEA) of the electrolyte membrane / electrode structure 34 is obtained from the variation of the tightening load W (ALL) applied to the plurality of fuel cells 22 in the stacking direction. The water content of the electrolyte membrane / electrode structure 34 is calculated. For this reason, it becomes possible to accurately and reliably estimate the water content of the electrolyte membrane / electrode structure 34 regardless of the state of the fuel cell stack 10, for example, during operation or stoppage.

  Thereby, the membrane water content of the electrolyte membrane / electrode structure 34 can be accurately estimated by a simple process, and the electrolyte membrane / electrode structure 34 can be maintained in an efficient state. Therefore, it is possible to improve the power generation performance, suppress the durability deterioration, and obtain the effect that the operation control of the fuel cell stack 10 can be satisfactorily performed based on the membrane water content.

  After the membrane water content of the electrolyte membrane / electrode structure 34 is calculated, the process proceeds to step S4, and it is determined whether or not the membrane water content is within the set target width. When it is determined that the membrane water content is within the set target width (YES in step S4), the membrane water content measurement step is completed. On the other hand, if it is determined that the membrane water content is not within the set target width (NO in step S4), the process proceeds to step S5.

  If it is determined that the water content of the membrane is larger than the set target width (YES in step S5), the process proceeds to step S6, and the temperature of the cooling medium is detected via the sensor 114c that constitutes the cooling medium supply device 18. It is determined whether or not the temperature of the cooling medium is lower than a set target temperature. If it is determined that the temperature of the cooling medium is lower than the set target temperature (YES in step S6), the process proceeds to step S7, and the cooling medium flow rate is decreased.

  Specifically, as shown in FIG. 1, the refrigerant pump 112 constituting the cooling medium supply device 18 is controlled, and the flow rate of the cooling medium circulated and supplied to the fuel cell stack 10 is reduced. For this reason, the internal temperature of the fuel cell stack 10 increases, and the membrane water content of the electrolyte membrane / electrode structure 34 decreases.

  If it is determined that the temperature of the cooling medium is higher than the set target temperature (NO in step S6), the process proceeds to step S8. In step S8, the state of charge of the battery 21 is monitored, and if it is determined that the remaining amount of the battery 21 is lower than the target (YES in step S8), the process proceeds to step S9. In step S9, the pressure reducing valve 84 constituting the hydrogen supply device 14 and the air pump 98 constituting the air supply device 16 are controlled, and the flow rates of the fuel gas and the oxidant gas supplied to the fuel cell stack 10 are increased. As a result, the amount of water discharged from the water vapor inside the fuel cell stack 10 increases, and the membrane water content of the electrolyte membrane / electrode structure 34 decreases.

  If it is determined in step S8 that the remaining amount of the battery 21 is higher than the target (NO in step S8), the process proceeds to step S10, and the power generation amount of the fuel cell stack 10 is reduced. For this reason, the amount of water generated in the fuel cell stack 10 is reduced, and the membrane water content of the electrolyte membrane / electrode structure 34 is reduced.

On the other hand, when it is determined in step S5 that the membrane water content is smaller than the set target width (for example, 0.2 g / cm ³ or more and the saturated water content or less) that is a water content range in which power generation performance is good. (NO in step S5), the process proceeds to step S11, and it is determined whether or not the temperature of the cooling medium is higher than the set target temperature. If it is determined that the temperature of the cooling medium is higher than the set target temperature (YES in step S11), the process proceeds to step S12 to increase the cooling medium flow rate. Therefore, the temperature inside the fuel cell stack 10 decreases, and the membrane humidification amount of the electrolyte membrane / electrode structure 34 increases.

  If it is determined in step S11 that the temperature of the cooling medium is lower than the set target temperature (NO in step S11), the process proceeds to step S13. If it is determined in step S13 that the remaining amount of the battery 21 is higher than the target (YES in step S13), the process proceeds to step S14. In step S14, the flow rates of the fuel gas and the oxidant gas supplied to the fuel cell stack 10 are decreased. For this reason, the flow rate of water vapor in the fuel cell stack 10 decreases, and the membrane humidification amount of the electrolyte membrane / electrode structure 34 increases.

  If it is determined in step S13 that the remaining amount of the battery 21 is lower than the target (NO in step S13), the process proceeds to step S15, and the power generation amount of the fuel cell stack 10 is increased. Therefore, the battery 21 is charged or the current is supplied to the load, the amount of moisture generated in the fuel cell stack 10 is increased, and the amount of membrane humidification of the electrolyte membrane / electrode structure 34 is increased.

  Thereby, in this embodiment, the membrane water content of the electrolyte membrane / electrode structure 34 can be maintained within the set target width during operation, and an efficient state for the electrolyte membrane / electrode structure 34 is maintained. It becomes possible to do. Therefore, there is an advantage that the power generation performance of the electrolyte membrane / electrode structure 34 can be improved and durability deterioration can be suppressed as much as possible.

  In the present embodiment, when the operation of the fuel cell stack 10 is stopped, the process is performed along the above process (along FIG. 11) when stopping the membrane water content within the set target width. It can be carried out.

FIG. 12 is another flowchart for explaining a control method when the fuel cell stack 10 is stopped (when the ignition is off). Detailed description of the same steps as those in the flowchart shown in FIG. 11 is omitted.

  After the tightening load W (ALL) of the fuel cell stack 10 is detected (Step S21), the processes up to Step S24 are performed in the same manner as Steps S1 to S4. If it is determined that the membrane water content is not within the set target width (NO in step S24), the process proceeds to step S25, where it is determined whether or not the membrane water content is greater than the set target width.

  If it is determined that the membrane water content is larger than the set target width (YES in step S25), the process proceeds to step S26, and the flow rates of the fuel gas and the oxidant gas supplied to the fuel cell stack 10 are increased. . For this reason, the discharge amount of water vapor inside the fuel cell stack 10 increases, and the membrane water content of the electrolyte membrane / electrode structure 34 decreases.

  On the other hand, when it is determined that the membrane water content is smaller than the set target width (NO in step S25), the process proceeds to step S27, and the fuel cell stack 10 is generated for a certain period of time. Thereby, produced water is obtained by the power generation reaction, and the membrane water content of the electrolyte membrane / electrode structure 34 increases.

  Therefore, when the operation of the fuel cell stack 10 is stopped, the operation of the fuel cell stack 10 can be stopped while maintaining the membrane water content within the set target width, and the durability of the solid polymer electrolyte membrane 56 is improved. It becomes possible to make it.

  The load sensor is not limited to the load cell 72. For example, a strain gauge may be provided on the bar or bolt passed between the pair of end plates 28a, 28b, and the load value measured from each strain gauge may be added together.

DESCRIPTION OF SYMBOLS 10 ... Fuel cell stack 12 ... Fuel cell system 14 ... Hydrogen supply device 16 ... Air supply device 18 ... Cooling medium supply device 20 ... ECU
DESCRIPTION OF SYMBOLS 22 ... Fuel cell 24 ... Laminated body 25a, 25b ... Terminal plate 26a, 26b ... Insulating plate 28a, 28b ... End plate 30 ... Load measuring mechanism 32 ... Pressurizing mechanism 34 ... Electrolyte membrane electrode assembly 36, 38 ... Separator 40a ... Oxidant gas inlet communication hole 40b ... Oxidant gas outlet communication hole 42a ... Fuel gas inlet communication hole 42b ... Fuel gas outlet communication hole 44a ... Cooling medium inlet communication hole 44b ... Cooling medium outlet communication hole 46 ... Oxidant gas flow path DESCRIPTION OF SYMBOLS 48 ... Fuel gas flow path 50 ... Cooling medium flow path 56 ... Solid polymer electrolyte membrane 58 ... Cathode side electrode 60 ... Anode side electrode 61 ... Connection bar 64 ... Pressure plate 68 ... Connection member 72 ... Load cell 76 ... Pressing member 78 ... Load adjustment bolt 80 ... Hydrogen tank 86 ... Ejector 88 ... Hydrogen circulation path 90 ... Gas-liquid separator 98 ... Air pump 112 ... Cool Medium pump 114a, 114b, 114c ... sensor

Claims (2)

An electrolyte membrane / electrode structure provided with electrodes on both sides of the electrolyte membrane and a separator are stacked with a seal member interposed therebetween, and power is generated by the supplied fuel gas and oxidant gas, and cooling is supplied. A fuel cell stack control method comprising a fuel cell cooled by a medium, wherein a plurality of the fuel cells are stacked,
Wherein when changing the load current of the fuel cell, corresponding to the actually measured clamping force, the sealing member to the applied load applied in the stacking direction, of the working pressure load and membrane load in the stacking direction based on the operating pressure Storing the relationship in a table;
Measuring the tightening load applied to the plurality of fuel cells in the stacking direction;
A step asking you to the film load based on said tightening load using the table were measured,
And calculating the water content of the electrolyte membrane before Kimaku load,
Adjusting at least one of the flow rate of the fuel gas and the oxidant gas, the flow rate of the cooling medium, or the power generation amount based on the calculated water content and the temperature of the cooling medium;
A method for controlling a fuel cell stack, comprising: 2. The control method according to claim 1, wherein the fuel cell stack includes a pair of end plates disposed at both ends in a stacking direction of the plurality of the fuel cells, and the pair of end plates is integrated with each other while maintaining a separation distance therebetween. And fixed to
A method for controlling a fuel cell stack, wherein a load measuring mechanism for providing a plurality of load sensors is disposed between the pair of end plates.

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