JP2011034868A - Fuel cell - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To readily and surely discharge standing water from within a separator plane, using a simple and compact structure. <P>SOLUTION: The fuel cell 10 is constituted by horizontally laminating a plurality of power generation units 12. An outlet buffer unit communicating with an oxidizer gas outlet communicating hole 30b is disposed downstream of an oxidizer gas flow passage 50 and a drainage communication hole 68, communicating with the outlet buffer unit, to discharge the water generated is formed. In an oxidizer gas outlet manifold 80b, communicating with the oxidizer gas outlet communicating hole 30b, a suction port 98 of a venturi tube 88 communicates with a manifold outlet 86a of a drainage manifold 86, that communicates with the drainage communication hole 68. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

  The present invention includes a plurality of power generation units in which an electrolyte / electrode structure in which a pair of electrodes are provided on both sides of an electrolyte and a separator are stacked, and a fuel gas or The present invention relates to a fuel cell in which a reaction gas flow path for supplying a reaction gas that is an oxidant gas is provided, and a reaction gas supply communication hole and a reaction gas discharge communication hole through which the reaction gas flows are provided.

  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 provided by a pair of separators. It has a power generation unit that is sandwiched. This type of fuel cell is normally used as a fuel cell stack by stacking a predetermined number of power generation units.

  In the above fuel cell, a fuel gas flow channel for flowing fuel gas is provided in the plane of one separator so as to face the anode side electrode, and the cathode side electrode is opposed in the plane of the other separator. An oxidant gas flow path for flowing an oxidant gas is provided. Further, between the separators adjacent to each other, a cooling medium flow path for flowing the cooling medium is provided along the surface direction of the separator.

  Further, in this type of fuel cell, a fuel gas inlet communication hole and a fuel gas outlet communication hole for flowing fuel gas through the power generation unit in the stacking direction, and an oxidant gas inlet communication hole for flowing oxidant gas In many cases, a so-called internal manifold type fuel cell is provided which includes an oxidant gas outlet communication hole, a cooling medium inlet communication hole for flowing a cooling medium, and a cooling medium outlet communication hole.

  As an internal manifold type fuel cell, for example, a polymer electrolyte fuel cell disclosed in Patent Document 1 is known. In this fuel cell, as shown in FIG. 7, a plurality of anode side channels 1 are formed along the vertical direction, and a water distribution substrate 2 and a gas distribution substrate are disposed upstream of the anode side channel 1. 3 is disposed. The water distribution substrate 2 and the gas distribution substrate 3 are each formed with a plurality of pores 2 a and 3 a, and the pores 2 a and 3 a communicate with the anode side flow path 1.

  A pair of water introduction manifold holes 4a and 4a and fuel gas introduction manifold holes 5a and 5a are formed on both sides of the upper side of the fuel cell. A pair of manifold holes 5b and 5b for deriving fuel gas and manifold holes 4b and 4b for deriving water are formed on both sides of the lower side of the fuel cell.

  Water is supplied from a water pump 6 to the water introduction manifold holes 4a and 4a, while fuel gas is supplied from a hydrogen gas cylinder 7 to the fuel gas introduction manifold holes 5a and 5a. The water outlet manifold holes 4b and 4b and the fuel gas outlet manifold holes 5b and 5b communicate with the separation tank 8, and the water stored in the separation tank 8 is cooled by the cooler 9. The water is supplied to the manifold holes 4a and 4a through the water pump 6.

Japanese Patent No. 3123992

  In the above-mentioned Patent Document 1, water contained in the fuel gas used for the reaction through the anode side flow path 1 is led to the manifold holes 4b and 4b and sent to the separation tank 8, while this used Water contained in the fuel gas is introduced into the separation tank 8 and separated from the fuel gas.

  However, the downstream side (lower end portion side) of the anode-side channel 1 has a problem that water is particularly likely to stay and it is difficult to reliably discharge a large amount of the staying water.

  In addition, each of the fuel cells includes a pair of water introduction manifold holes 4a and 4a, a fuel gas introduction manifold hole 5a and 5a, a water discharge manifold hole 4b and 4b, and a fuel gas discharge manifold hole 5b, 5b is provided. For this reason, there is a problem that the configuration of the entire fuel cell is complicated, the fuel cell is increased in size, and the cost is increased.

  The present invention solves this type of problem, and an object thereof is to provide a fuel cell capable of easily and reliably discharging stagnant water from the separator surface with a simple and compact configuration.

  The present invention includes a plurality of power generation units in which an electrolyte / electrode structure in which a pair of electrodes are provided on both sides of an electrolyte and a separator are stacked, and a fuel gas or The present invention relates to a fuel cell in which a reaction gas flow path for supplying a reaction gas that is an oxidant gas is provided, and a reaction gas supply communication hole and a reaction gas discharge communication hole through which the reaction gas flows are provided. is there.

  In this fuel cell, an outlet buffer portion communicating with the reaction gas discharge communication hole is provided at a downstream portion of the reaction gas flow path, and a drain communication hole for discharging the generated water in communication with the outlet buffer portion is laminated. The reaction gas outlet manifold that is formed in the direction and communicates with the reaction gas discharge communication hole is provided with a venturi that communicates with the suction port at the outlet of the discharge manifold that communicates with the drain communication hole.

  In the fuel cell, it is preferable that end plates are disposed at both ends of the power generation unit in the stacking direction, and a venturi is integrally disposed on one of the end plates.

  Further, the venturi is partitioned into a negative pressure chamber and a pressurization chamber that communicate with the suction port via a diaphragm, and the reaction gas inlet manifold that communicates with the reaction gas supply communication hole communicates with the pressurization chamber. Is preferred.

  According to the present invention, the reaction gas outlet manifold is provided with the venturi, and the venturi suction port communicates with the outlet of the drainage manifold communicating with the outlet buffer portion.

  For this reason, a negative pressure is generated at the suction port of the venturi by the flow rate of the reaction gas flowing through the reaction gas outlet manifold. Accordingly, the outlet of the drainage manifold is sucked, and the generated water can be smoothly and reliably discharged from the drainage manifold to the reaction gas outlet manifold.

1 is a schematic perspective view of a fuel cell according to an embodiment of the present invention. It is a principal part disassembled perspective explanatory drawing of the electric power generation unit which comprises the said fuel cell. FIG. 3 is a sectional view of the fuel cell taken along line III-III in FIG. 2. It is front explanatory drawing of the 2nd separator which comprises the said electric power generation unit. It is principal part cross-sectional explanatory drawing of the said fuel cell. It is operation | movement explanatory drawing of the venturi which comprises the said fuel cell. 2 is an explanatory diagram of a polymer electrolyte fuel cell disclosed in Patent Document 1. FIG.

  As shown in FIG. 1, a fuel cell 10 according to an embodiment of the present invention includes a power generation unit 12, and a plurality of the power generation units 12 are stacked together in a horizontal direction (arrow A direction), for example. Configure. In addition, the electric power generation unit 12 may be laminated | stacked on the gravitational direction (vertical direction).

  As shown in FIGS. 2 and 3, the power generation unit 12 includes a first separator 14, an electrolyte membrane / electrode structure (electrolyte / electrode structure) 16, and a second separator 18. The first separator 14 and the second separator 18 are made of, for example, a steel plate, a stainless steel plate, an aluminum plate, a plated steel plate, or a vertically long metal plate having a surface treated for anticorrosion on its metal surface.

  The first separator 14 and the second separator 18 have a rectangular planar shape, and are formed into a concavo-convex shape by pressing a metal thin plate into a wave shape. In addition, you may comprise the 1st separator 14 and the 2nd separator 18 with a carbon separator, for example.

  The electrolyte membrane / electrode structure 16 includes, for example, a solid polymer electrolyte membrane 22 in which a thin film of perfluorosulfonic acid is impregnated with water, and an anode side electrode 24 and a cathode side electrode 26 that sandwich the solid polymer electrolyte membrane 22. With. The anode side electrode 24 constitutes a so-called stepped MEA having a smaller surface area than the cathode side electrode 26.

  The anode side electrode 24 and the cathode side electrode 26 are uniformly coated on the surface of the gas diffusion layer with a gas diffusion layer (not shown) made of carbon paper or the like and porous carbon particles carrying a platinum alloy on the surface. And an electrode catalyst layer (not shown) formed. The electrode catalyst layers are formed on both surfaces of the solid polymer electrolyte membrane 22.

  As shown in FIG. 2, the upper end edge of the power generation unit 12 in the long side direction (arrow C direction) communicates with each other in the arrow A direction to oxidize for supplying an oxidant gas, for example, an oxygen-containing gas. An agent gas inlet communication hole (reaction gas supply communication hole) 30a and a fuel gas inlet communication hole (reaction gas supply communication hole) 32a for supplying a fuel gas, for example, a hydrogen-containing gas, are provided.

  A fuel gas outlet communication hole (reactive gas discharge communication hole) 32b for discharging fuel gas to communicate with each other in the arrow A direction at the lower edge of the long side direction (arrow C direction) of the power generation unit 12, and An oxidant gas outlet communication hole (reaction gas discharge communication hole) 30b for discharging the oxidant gas is provided.

  At one edge of the power generation unit 12 in the short side direction (arrow B direction), there is provided a cooling medium inlet communication hole 34a that communicates with each other in the direction of arrow A and supplies a cooling medium. A cooling medium outlet communication hole 34b for discharging the cooling medium is provided at the other end edge in the short side direction.

  On the surface 14a of the first separator 14 facing the electrolyte membrane / electrode structure 16, a fuel gas flow path (reactive gas flow path) 36 that connects the fuel gas inlet communication hole 32a and the fuel gas outlet communication hole 32b is formed. The The fuel gas channel 36 has a plurality of wave-like channel grooves 36a extending in the direction of arrow C, and an inlet buffer unit 38 having a plurality of embosses in the vicinity of the inlet and the outlet of the fuel gas channel 36, respectively. And an outlet buffer 40 is provided.

  On the surface 14b of the first separator 14, a plurality of flow channel grooves 44a that are part of the cooling medium flow channel 44 that communicates the cooling medium inlet communication hole 34a and the cooling medium outlet communication hole 34b are formed. An inlet buffer portion 46a and an outlet buffer portion 48a each having a plurality of embosses are provided in the vicinity of the inlet and the outlet of the channel groove 44a.

  On the surface 18a of the second separator 18 facing the electrolyte membrane / electrode structure 16, as shown in FIG. 4, an oxidant gas flow path that connects the oxidant gas inlet communication hole 30a and the oxidant gas outlet communication hole 30b. (Reactive gas flow path) 50 is formed. The oxidant gas channel 50 has a plurality of wave-like channel grooves 50a extending in the direction of arrow C. An inlet buffer portion 52 and an outlet buffer portion 54 are provided in the vicinity of the inlet and the outlet of the oxidizing gas channel 50.

  As shown in FIG. 2, a plurality of flow channel grooves 44 b that are a part of the cooling medium flow channel 44 are formed on the surface 18 b of the second separator 18. An inlet buffer portion 46b and an outlet buffer portion 48b each having a plurality of embosses are provided in the vicinity of the inlet and outlet of the channel groove 44b.

  As shown in FIGS. 2 and 3, first seal members 56 are individually or integrally provided on the surfaces 14 a and 14 b of the first separator 14 around the outer peripheral edge of the first separator 14. . On the surfaces 18a and 18b of the second separator 18, a second seal member 58 is provided individually or integrally around the outer peripheral edge of the second separator 18.

  The first separator 14 includes a plurality of supply holes 60a that communicate with the fuel gas inlet communication hole 32a and the fuel gas flow path 36, and a plurality of discharge holes that communicate with the fuel gas outlet communication hole 32b and the fuel gas flow path 36. 60b.

  As shown in FIG. 4, the second separator 18 includes a plurality of inlet side connection flow paths 62 a at the communication portion between the oxidant gas inlet communication hole 30 a and the oxidant gas outlet communication hole 30 b and the oxidant gas flow path 50. And the some receiving part 64a and 64b which form the some exit side connection flow path 62b are provided.

  In the first separator 14 and the second separator 18, drainage communication holes 66 and 68 are formed in the stacking direction adjacent to the oxidant gas outlet communication hole 30 b and the fuel gas outlet communication hole 32 b. The drain communication hole 66 communicates with the outlet buffer portion 40 of the fuel gas flow path 36 and discharges generated water, while the drain communication hole 68 communicates with the outlet buffer section 54 of the oxidant gas flow path 50 to generate water. (See FIGS. 2 and 4).

  As the power generation units 12 are stacked on each other, a cooling medium flow path 44 is formed between the first separator 14 constituting one power generation unit 12 and the second separator 18 constituting the other power generation unit 12. It is formed.

  As shown in FIG. 1, in the fuel cell 10, a first terminal plate 70 a, a first insulating plate 72 a, and a first end plate 74 a are stacked at one end in the stacking direction of the plurality of power generation units 12. At the other end of the fuel cell 10 in the stacking direction, a second terminal plate 70b, a second insulating plate 72b, and a second end plate 74b are stacked.

  The first end plate 74a and the second end plate 74b configured in a rectangular shape are integrally clamped and held by a plurality of tie rods (not shown) extending in the arrow A direction. The fuel cell 10 may be integrally held by a box-shaped casing (not shown) including the first end plate 74a and the second end plate 74b as end plates.

  An oxidant gas inlet manifold (reactive gas inlet manifold) 80a that communicates with the oxidant gas inlet communication hole 30a and a fuel gas inlet manifold (reactive gas) that communicates with the fuel gas inlet communication hole 32a are provided at the top of the first end plate 74a. An inlet manifold) 82a is formed therethrough. On the lower side of the first end plate 74a, an oxidant gas outlet manifold (reaction gas outlet manifold) 80b communicating with the oxidant gas outlet communication hole 30b and a fuel gas outlet manifold (reaction) communicating with the fuel gas outlet communication hole 32b are provided. Gas outlet manifold) 82b.

  A cooling medium inlet manifold 84a that communicates with the cooling medium inlet communication hole 34a and a cooling medium outlet manifold 84b that communicates with the cooling medium outlet communication hole 34b are formed through the second end plate 74b.

  As shown in FIG. 5, a drain manifold 86 that communicates with the drain communication hole 68 is formed in the first end plate 74 a. One end of the drainage manifold 86 communicates with each drainage communication hole 68 of the power generation unit 12, and the other end is curved or bent from the horizontal direction (arrow A direction) to the vertical downward direction (arrow C direction). Open to the outlet manifold 80b.

  The oxidant gas outlet manifold 80b is formed in a tapered shape so that the opening width dimension decreases outwardly from the oxidant gas outlet communication hole 30b, while the manifold of the drainage manifold 86 is formed on the first end plate 74a. A venturi 88 is disposed opposite the outlet 86a.

  The venturi 88 includes a housing 90 that is integrated with the first end plate 74a. In the housing 90, the piston 92 is accommodated in the oxidant gas outlet manifold 80b so as to be able to advance and retract, and between the receiving portion 94 provided on the tip end side of the piston 92 and the bottom surface of the housing 90, A spring 96 is interposed.

  The oxidant gas outlet manifold 80b has, for example, a tapered hole portion so that the opening cross-sectional area decreases outward from the oxidant gas outlet communication hole 30b.

  The spring 96 abuts on the receiving portion 94 to hold the piston 92 in a state of protruding into the oxidant gas outlet manifold 80b. A small-diameter suction port 98 is formed at the tip of the piston 92, and the suction port 98 opens into the oxidant gas outlet manifold 80b. A diaphragm 100 is attached between the rear end portion of the piston 92 and the inner wall surface of the housing 90.

  The venturi 88 is partitioned into a negative pressure chamber 102 communicating with the suction port 98 via the diaphragm 100 and a pressurization chamber 104. The oxidant gas inlet manifold 80 a and the pressurizing chamber 104 communicate with each other via the pressure pipe 106. The casing 90 is provided with an air bend unit 108 to which the pressure pipe 106 is connected.

  Although not shown, the drain communication hole 66 that communicates with the outlet buffer section 40 of the fuel gas flow path 36 and discharges the generated water communicates with the outlet buffer section 54 of the oxidant gas flow path 50 to generate the generated water. In the same manner as the drainage communication hole 68 that discharges water, it communicates with the drainage manifold and is sucked by the venturi.

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

  First, as shown in FIG. 1, an oxidant gas such as an oxygen-containing gas is supplied from an oxidant gas inlet manifold 80a of the first end plate 74a to the oxidant gas inlet communication hole 30a, and a fuel gas inlet manifold. Fuel gas such as hydrogen-containing gas is supplied from 82a to the fuel gas inlet communication hole 32a.

  Further, a cooling medium such as pure water or ethylene glycol oil is supplied from the cooling medium inlet manifold 84a of the second end plate 74b to the cooling medium inlet communication hole 34a.

  Therefore, as shown in FIG. 2, the oxidant gas is introduced into the oxidant gas flow path 50 of the second separator 18 from the oxidant gas inlet communication hole 30a. The oxidant gas moves in the direction of arrow C (gravity direction) along the oxidant gas flow path 50 and is supplied to the cathode side electrode 26 of the electrolyte membrane / electrode structure 16 (see FIG. 4).

  On the other hand, as shown in FIG. 3, the fuel gas moves from the fuel gas inlet communication hole 32a to the surface 14a side of the first separator 14 through the supply hole 60a. The fuel gas moves in the gravitational direction (arrow C direction) along the fuel gas flow path 36 and is supplied to the anode electrode 24 of the electrolyte membrane / electrode structure 16 (see FIGS. 2 and 3).

  Therefore, in the electrolyte membrane / electrode structure 16, the oxidant gas supplied to the cathode side electrode 26 and the fuel gas supplied to the anode side electrode 24 are consumed by an electrochemical reaction in the electrode catalyst layer to generate power. Is done.

  Next, the oxidant gas supplied and consumed to the cathode electrode 26 of the electrolyte membrane / electrode structure 16 is discharged in the direction of arrow A along the oxidant gas outlet communication hole 30b. On the other hand, the fuel gas supplied and consumed to the anode side electrode 24 of the electrolyte membrane / electrode structure 16 is led to the surface 14b side of the first separator 14 through the discharge hole 60b. The fuel gas led out to the surface 14b side is discharged to the fuel gas outlet communication hole 32b.

  Further, as shown in FIGS. 2 and 3, the cooling medium supplied to the cooling medium inlet communication hole 34 a includes the first separator 14 constituting one power generation unit 12 and the second separator constituting the other power generation unit 12. It is introduced into a cooling medium flow path 44 formed between the separator 18.

  Thereby, the cooling medium supplied from the cooling medium inlet communication hole 34a to the cooling medium flow path 44 moves in the direction of arrow B to cool the power generation unit 12, and then is discharged to the cooling medium outlet communication hole 34b.

  In this case, in the present embodiment, as shown in FIG. 5, a venturi 88 is provided in the oxidant gas outlet manifold 80b, and a suction port 98 of the venturi 88 protrudes into the oxidant gas outlet manifold 80b and is a drainage manifold. It communicates with 86 manifold outlets 86a.

  For this reason, a negative pressure is generated at the suction port 98 of the venturi 88 due to the flow rate of the exhaust oxidant gas flowing through the oxidant gas outlet manifold 80b. Accordingly, the manifold outlet 86a of the drainage manifold 86 is sucked, and the produced water can be smoothly and reliably discharged from the drainage communication hole 68 through which the drainage manifold 86 communicates to the oxidant gas outlet manifold 80b.

  Further, as shown in FIG. 4, the drain communication hole 68 is provided at a position below the outlet buffer portion 54 that communicates with the lower end portion (downstream side) of the oxidant gas flow path 50. As a result, the reaction product water is discharged to the drain communication hole 68 through gravity, and the product water discharged from the oxidant gas flow path 50 of each power generation unit 12 is sucked into the drain manifold 86 and is discharged to the oxidant gas outlet. It is discharged to the manifold 80b.

  Further, the generated water in the fuel gas passage 36 is discharged to the drain communication hole 66, and is smoothly and reliably discharged from a discharge manifold (not shown) to the fuel gas outlet manifold 82b via the Belche.

  Incidentally, in the venturi 88, the pressurizing chamber 104 communicates with the oxidant gas inlet manifold 80a via the pressure pipe 106. For this reason, when the flow rate of the oxidant gas supplied to the fuel cell 10 is small, the pressure of the oxidant gas inlet manifold 80a decreases, and the pressure of the oxidant gas acting on the pressurizing chamber 104 decreases. On the other hand, in the oxidant gas outlet manifold 80b, the flow rate of the flowing oxidant gas decreases.

  Therefore, the negative pressure generated at the suction port 98 of the venturi 88 is reduced, and the pressure difference between the negative pressure chamber 102 and the pressurizing chamber 104 is reduced. As a result, the piston 92 protrudes in the direction of the arrow C1 (oxidant gas outlet manifold 80b side) in FIG. 6 via the elastic force of the spring 96. For this reason, the piston 92 largely protrudes toward the oxidant gas outlet manifold 80 b, and the suction port 98 is close to the manifold outlet 86 a of the drainage manifold 86.

  As a result, even when the flow rate of the oxidant gas flowing through the oxidant gas outlet manifold 80b is small, a negative pressure is generated at the suction port 98, and the generated water is sucked from the manifold outlet 86a into the oxidant gas outlet manifold 80b. Processing is performed well.

  On the other hand, when the flow rate of the oxidant gas supplied to the oxidant gas inlet manifold 80a increases, as shown in FIG. 5, the pressure of the oxidant gas introduced into the pressurization chamber 104 via the pressure pipe 106 is shown. Will increase. Furthermore, the flow rate of the oxidant gas flowing through the oxidant gas outlet manifold 80b increases, and the negative pressure generated in the negative pressure chamber 102 from the suction port 98 increases.

  As a result, the pressure difference between the negative pressure chamber 102 and the pressurizing chamber 104 increases, and the piston 92 moves in the direction of the arrow C2 (the direction away from the oxidant gas outlet manifold 80b) against the elastic force of the spring 96. To do. Therefore, the opening diameter of the oxidant gas outlet manifold 80b is enlarged by the piston 92, and the oxidant gas can be favorably distributed, and the generated water can be satisfactorily sucked from the manifold outlet 86a to the oxidant gas outlet manifold 80b. The advantage that it can be obtained.

  The fuel gas channel 36 is configured in the same manner as the oxidant gas channel 50, and the same effect as described above can be obtained.

DESCRIPTION OF SYMBOLS 10 ... Fuel cell 12 ... Electric power generation unit 14, 18 ... Separator 16 ... Electrolyte membrane electrode structure 22 ... Solid polymer electrolyte membrane 24 ... Anode side electrode 26 ... Cathode side electrode 30a ... Oxidant gas inlet communication hole 30b ... Oxidant Gas outlet communication hole 32a ... Fuel gas inlet communication hole 32b ... Fuel gas outlet communication hole 34a ... Cooling medium inlet communication hole 34b ... Cooling medium outlet communication hole 36 ... Fuel gas flow paths 38, 46a, 46b, 52 ... Inlet buffer section 40 , 48a, 48b, 54 ... outlet buffer section 44 ... cooling medium flow path 50 ... oxidant gas flow path 66, 68 ... drainage communication hole 74a, 74b ... end plate 80a ... oxidant gas inlet manifold 80b ... oxidant gas outlet manifold 82a ... Fuel gas inlet manifold 82b ... Fuel gas outlet manifold 88 ... Venturi 90 ... Housing 92 Piston 96 ... spring 98 ... suction port 100 ... Diaphragm 102 ... negative pressure chamber 104 ... pressurizing chamber 106 ... pressure tube

Claims (3)

A plurality of power generation units in which an electrolyte / electrode structure provided with a pair of electrodes on both sides of the electrolyte and a separator are stacked, and a fuel gas or an oxidant gas along the electrodes are provided on the electrode facing surface of the separator. A fuel cell is provided with a reaction gas flow path for supplying a reaction gas and a reaction gas supply communication hole and a reaction gas discharge communication hole through which the reaction gas flows in the stacking direction,
An outlet buffer part communicating with the reactive gas discharge communication hole is provided at a downstream portion of the reactive gas flow path, and a drain communication hole for discharging generated water in communication with the outlet buffer part is provided in the stacking direction. As it is formed,
The fuel cell according to claim 1, wherein the reaction gas outlet manifold communicating with the reaction gas discharge communication hole is provided with a venturi having a suction port communicating with an outlet of the drainage manifold communicating with the drainage communication hole. 2. The fuel cell according to claim 1, wherein the fuel cell has end plates disposed at both ends in the stacking direction of the power generation unit, and
The fuel cell according to claim 1, wherein the venturi is integrally disposed on one of the end plates. 3. The fuel cell according to claim 1, wherein the venturi is partitioned into a negative pressure chamber and a pressurization chamber that communicate with the suction port via a diaphragm.
A fuel cell, wherein a reaction gas inlet manifold communicating with the reaction gas supply communication hole communicates with the pressurizing chamber.

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