JP5886739B2 - Fuel cell stack - Google Patents

Description

  The present invention relates to a fuel cell stack having a fuel cell in which an electrolyte membrane / electrode structure provided with a pair of electrodes on both sides of an electrolyte membrane and a horizontally long separator are stacked, and a plurality of the fuel cells are stacked. .

  For example, in a polymer electrolyte fuel cell, an electrolyte membrane / electrode structure in which an anode electrode is provided on one side of an electrolyte membrane made of a polymer ion exchange membrane and a cathode electrode is provided on the other side of the electrolyte membrane ( MEA) is provided with a unit cell sandwiched by a pair of separators. This type of fuel cell is normally used as an in-vehicle fuel cell stack by stacking a predetermined number of unit cells.

  In the fuel cell described above, a fuel gas flow path is provided in the surface of one separator so as to flow the fuel gas so as to face the anode electrode, and oxidation is performed in the surface of the other separator so as to face the cathode electrode. An oxidant gas flow path for flowing the agent gas is provided. Furthermore, between each separator which comprises each fuel cell and adjoins mutually, the cooling medium flow path for flowing a cooling medium in the electrode range is formed along the separator surface.

  Further, in this type of fuel cell, the fuel gas inlet communication hole and the fuel gas outlet communication hole for flowing the fuel gas through the unit cell in the stacking direction, and the oxidant gas inlet communication hole for flowing the 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.

  However, the internal manifold type fuel cell has a problem that it is difficult to uniformly supply the reaction gas from the reaction gas communication hole to the entire surface of the reaction gas channel. Thus, for example, a fuel cell disclosed in Patent Document 1 is known.

  In this fuel cell, an electrolyte membrane / electrode structure provided with electrodes on both sides of an electrolyte membrane and a separator are laminated, a reaction gas flow path for supplying a reaction gas is formed along the electrode surface, and the reaction gas The reaction gas communication hole is formed to flow in the laminating direction.

  The separator is located on the inlet side of the reaction gas channel, and has a substantially triangular inlet buffer portion having a width dimension equivalent to that of the reaction gas channel, and a reaction gas located on one ridge line side of the inlet buffer portion And a supply side of the communication hole. The inlet buffer unit has a plurality of convex portions, and the convex portions are arranged such that the arrangement density on the central portion side of the inlet buffer portion is sparse compared to the arrangement density on the end side of the inlet buffer portion. Is set to

  Accordingly, the arrangement density of the protrusions is sparse particularly in the width direction central portion side of the inlet buffer portion where the reaction gas easily passes, so that the flow rate of the reaction gas is reduced and the reaction gas is reduced to the width of the reaction gas flow path. It can be guided to the flow path groove on the center side in the direction.

JP 2008-293743 A

  The present invention relates to this kind of technology, and with a simple and economical configuration, the reaction gas can be supplied uniformly over the entire surface of the reaction gas flow path, and the desired power generation performance can be ensured. An object of the present invention is to provide a simple fuel cell stack.

  The present invention has a fuel cell in which an electrolyte membrane / electrode structure in which electrodes are provided on both sides of an electrolyte membrane and a horizontally long separator are stacked, and a fuel gas or an oxidant gas is provided on the short side of the separator. A first reaction gas communication hole through which one of the reaction gases flows in the separator stacking direction, and a second reaction gas communication hole through which the other reaction gas of the fuel gas or the oxidant gas flows in the separator stacking direction And a fuel cell stack in which a plurality of the fuel cells are stacked.

In this fuel cell stack, the separator formed with the reaction gas flow path for flowing one reaction gas in the long side direction along the separator surface is the inlet side of the reaction gas flow path and the outlet side of the reaction gas flow path. Are provided with a triangular buffer part, respectively, and a plurality of connecting flow paths for connecting the first reaction gas communication hole and the buffer part are provided. The plurality of connection channels are channels directly connected along the separator surface from the first reaction gas communication hole to the buffer unit, and the channel length on the center side of the buffer unit is It is configured to be shorter than the flow path length on the end side of the buffer portion.

  In this fuel cell stack, the wall surface of the first reaction gas communication hole on the buffer portion side extends in a direction intersecting with each other with respect to a triangular ridge line facing the reaction gas communication hole of the buffer portion. It is preferable.

Further, in this fuel cell stack, the separator formed with the reaction gas flow path for allowing one reaction gas to flow in the long side direction along the separator surface includes the reaction gas flow path at the inlet side and the reaction gas flow path. In addition to providing a triangular buffer portion connected to each outlet side, a plurality of connecting flow paths for connecting the first reaction gas communication hole and the buffer portion are provided. The plurality of connection channels are channels directly connected along the separator surface from the first reaction gas communication hole to the buffer unit, and pressure loss on the center side of the buffer unit is caused by the buffer unit. The pressure loss is set to be smaller than the pressure loss on the end side.

  According to the present invention, the connection flow path is set such that the pressure loss on the center side of the buffer portion is smaller than the pressure loss on the end portion side of the buffer portion (hereinafter simply referred to as pressure loss). In the present invention, the flow path length on the center side of the buffer section is configured to be shorter than the flow path length on the end section side of the buffer section.

  For this reason, the pressure loss on the center side of the buffer portion is lower than the pressure loss on the end portion side of the buffer portion, and particularly increases the flow rate of the reaction gas supplied to the center side of the buffer portion where the reaction gas hardly flows. be able to. Therefore, the reaction gas can be supplied uniformly to the entire reaction gas flow path.

  Thereby, it is possible to supply the reaction gas evenly and reliably over the entire surface of the reaction gas flow path with a simple and economical configuration, and to secure desired power generation performance.

1 is an exploded perspective view of a main part of a fuel cell constituting a fuel cell stack according to a first embodiment of the present invention. FIG. 2 is a sectional view of the fuel cell taken along line II-II in FIG. 1. It is front explanatory drawing of the cathode side separator which comprises the said fuel cell. It is front explanatory drawing of the anode side separator which comprises the said fuel cell. It is comparison explanatory drawing of the flow volume of oxidant gas supplied to an oxidant gas flow path in the example of this application, and a prior art example. It is principal part explanatory drawing of the oxidant gas inlet communication hole which comprises the said fuel cell. It is front explanatory drawing of the cathode side separator which comprises the fuel cell stack which concerns on the 2nd Embodiment of this invention.

  As shown in FIGS. 1 and 2, the fuel cell stack 10 according to the first embodiment of the present invention includes a plurality of fuel cells 11 in the standing direction (the electrode surface is parallel to the vertical direction) in the arrow A direction. Laminated. The fuel cell 11 includes an electrolyte membrane / electrode structure 12, and a cathode side separator 14 and an anode side separator 16 that sandwich the electrolyte membrane / electrode structure 12.

  The cathode side separator 14 and the anode side separator 16 are made of, for example, a steel plate, a stainless steel plate, an aluminum plate, a plated steel plate, or a thin plate-like metal separator whose surface is subjected to anticorrosion treatment. The metal separator has a rectangular planar shape, and is formed into a concavo-convex shape by pressing into a wave shape. The cathode side separator 14 and the anode side separator 16 may be constituted by, for example, a carbon separator instead of the metal separator.

  The cathode-side separator 14 and the anode-side separator 16 have a horizontally long shape, and the short sides are directed in the direction of gravity (arrow C direction) and the long sides are directed in the horizontal direction (arrow B direction) (horizontal stacking). Composed. In addition, you may comprise so that a short side may face a horizontal direction and a long side may go to a gravitational direction.

  One end edge (one short side) of the fuel cell 11 in the long side direction (arrow B 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 18a and a fuel gas outlet communication hole 20b for discharging a fuel gas, for example, a hydrogen-containing gas, are provided. The oxidant gas inlet communication hole 18a and the fuel gas outlet communication hole 20b have a substantially rectangular shape (may be substantially triangular), and the oxidant gas inlet communication hole 18a is larger than the fuel gas outlet communication hole 20b. The opening area is set.

  The other end edge of the fuel cell 11 in the long side direction (the other short side) communicates with each other in the direction of the arrow A, and a fuel gas inlet communication hole 20a for supplying fuel gas, and an oxidant gas. An oxidant gas outlet communication hole 18b for discharging is provided. The oxidant gas outlet communication hole 18b and the fuel gas inlet communication hole 20a have a substantially rectangular shape, and the oxidant gas outlet communication hole 18b is set to have a larger opening area than the fuel gas inlet communication hole 20a.

  Two cooling medium inlet communication holes 22 a for communicating with each other in the direction of arrow A and for supplying a cooling medium are provided at one end of both ends in the short side direction (arrow C direction) of the fuel cell 11. Two cooling medium outlet communication holes 22b for discharging the cooling medium are provided on the other end of both ends in the short side direction of the fuel cell 11.

  The cooling medium inlet communication hole 22 a is set to have an approximately rectangular shape whose opening shape is long along the flow direction (arrow B direction) of the cooling medium flow path 38. The cooling medium outlet communication hole 22 b is set to have an approximately rectangular shape whose opening shape is long along the flow direction (arrow B direction) of the cooling medium flow path 38.

  The electrolyte membrane / electrode structure 12 includes, for example, a fluorine-based or hydrocarbon-based solid polymer electrolyte membrane 24, and a cathode electrode 26 and an anode electrode 28 that sandwich the solid polymer electrolyte membrane 24.

  The cathode electrode 26 and the anode electrode 28 are formed by uniformly applying a gas diffusion layer (not shown) made of carbon paper or the like and porous carbon particles carrying a platinum alloy on the surface thereof to the surface of the gas diffusion layer. And an electrode catalyst layer (not shown) to be formed. The electrode catalyst layers are formed on both surfaces of the solid polymer electrolyte membrane 24.

  As shown in FIG. 3, on the surface 14a of the cathode-side separator 14 facing the electrolyte membrane / electrode structure 12, an oxidant gas flow path that connects an oxidant gas inlet communication hole 18a and an oxidant gas outlet communication hole 18b. 30 is formed. The oxidant gas channel 30 extends in the horizontal direction (arrow B direction), and has a plurality of linear or wavy channel grooves 30a that circulate the oxidant gas in the long side direction along the separator surface.

  An inlet buffer portion 32 a and an outlet buffer portion 32 b each having a plurality of protruding embosses are provided in the vicinity of the inlet and the outlet of the oxidant gas flow path 30. The inlet buffer portion 32a has a substantially triangular shape along the shapes of the oxidant gas inlet communication hole 18a and the fuel gas outlet communication hole 20b, and the position of the apex 32ae is spaced downward from the center in the height direction (arrow C direction). Is set.

  The inlet buffer portion 32a has a first ridge line 32ar1 facing the oxidant gas inlet communication hole 18a and a second ridge line 32ar2 facing the fuel gas outlet communication hole 20b. The first ridgeline 32ar1 is configured to be longer than the second ridgeline 32ar2.

  The first ridge line 32ar1 extends non-parallel to the wall surface 18aw on the inlet buffer portion 32a side of the oxidant gas inlet communication hole 18a, that is, extends in a direction intersecting with each other. The distance between the first ridgeline 32ar1 and the wall surface 18aw becomes wider toward the upper side.

  The outlet buffer 32b has a substantially triangular shape along the shapes of the oxidant gas outlet communication hole 18b and the fuel gas inlet communication hole 20a, and the position of the apex 32be is spaced upward from the center in the height direction (arrow C direction). Is set. The outlet buffer portion 32b has a first ridge line 32br1 facing the oxidant gas outlet communication hole 18b and a second ridge line 32br2 facing the fuel gas inlet communication hole 20a. The first ridgeline 32br1 is configured to be longer than the second ridgeline 32br2.

  The first ridge line 32br1 extends non-parallel to the wall surface 18bw on the outlet buffer portion 32b side of the oxidant gas outlet communication hole 18b, that is, extends in a direction crossing each other. The distance between the first ridgeline 32br1 and the wall surface 18bw becomes wider toward the lower side.

  The inlet buffer portion 32a and the oxidant gas inlet communication hole 18a communicate with each other through a plurality of inlet connection channels 33a. The outlet buffer portion 32b and the oxidant gas outlet communication hole 18b communicate with each other through a plurality of outlet connection channels 33b. The inlet connection channel 33a and the outlet connection channel 33b have the same cross-sectional area cut in the direction intersecting the gas flow direction of each channel.

  The plurality of inlet connection channels 33a have a channel length L1 on the center side (vertex 32ae side) of the inlet buffer portion 32a that is greater than a channel length L2 on the end side (upper end side) of the inlet buffer portion 32a. Is also configured to be short (L1 <L2). In the plurality of outlet connection channels 33b, the channel length L3 on the center side (vertex 32be side) of the outlet buffer portion 32b is greater than the channel length L4 on the end portion side (lower end side) of the outlet buffer portion 32b. Is also configured to be short (L3 <L4).

  As shown in FIG. 4, a fuel gas flow path 34 that connects the fuel gas inlet communication hole 20 a and the fuel gas outlet communication hole 20 b is formed on the surface 16 a of the anode separator 16 facing the electrolyte membrane / electrode structure 12. Is done. The fuel gas channel 34 extends in the horizontal direction (arrow B direction), and has a plurality of linear or wavy channel grooves 34a that allow the fuel gas to flow in the long side direction along the separator surface. In the vicinity of the inlet and the outlet of the fuel gas channel 34, an inlet buffer portion 36a and an outlet buffer portion 36b each having a plurality of protruding embosses are provided.

  The inlet buffer 36a has a substantially triangular shape along the shapes of the fuel gas inlet communication hole 20a and the oxidant gas outlet communication hole 18b, and the position of the horizontal apex 36ae from the center in the height direction (arrow C direction). It is set apart upward.

  The inlet buffer portion 36a has a first ridge line 36ar1 facing the fuel gas inlet communication hole 20a and a second ridge line 36ar2 facing the oxidant gas outlet communication hole 18b. The first ridge line 36ar1 is configured to be shorter than the second ridge line 36ar2.

  The first ridge line 36ar1 extends non-parallel to the wall surface 20aw on the inlet buffer portion 36a side of the fuel gas inlet communication hole 20a, that is, extends in a direction crossing each other. The distance between the first ridge line 36ar1 and the wall surface 20aw becomes wider toward the upper side.

  The outlet buffer portion 36b has a substantially triangular shape along the shapes of the fuel gas outlet communication hole 20b and the oxidant gas inlet communication hole 18a, and the position of the vertex 36be is spaced downward from the center in the height direction (arrow C direction). Is set. The outlet buffer portion 36b has a first ridge line 36br1 facing the fuel gas outlet communication hole 20b and a second ridge line 36br2 facing the oxidant gas inlet communication hole 18a. The first ridge line 36br1 is configured to be shorter than the second ridge line 36br2.

  The first ridge line 36br1 extends non-parallel to the wall surface 20bw on the outlet buffer part 36b side of the fuel gas outlet communication hole 20b, that is, in a direction intersecting with each other. The distance between the first ridge line 36br1 and the wall surface 20bw becomes wider toward the lower side.

  The inlet buffer portion 36a and the fuel gas inlet communication hole 20a communicate with each other through a plurality of inlet connection channels 37a. The outlet buffer portion 36b and the fuel gas outlet communication hole 20b communicate with each other through a plurality of outlet connection channels 37b. The inlet connection channel 37a and the outlet connection channel 37b have the same cross-sectional area cut in the direction intersecting the gas flow direction of each channel.

  In the plurality of inlet connection channels 37a, the channel length L5 on the center side (vertex 36ae side) of the inlet buffer portion 36a is greater than the channel length L6 on the end side (upper end side) of the inlet buffer portion 36a. Is also configured to be short (L5 <L6). In the plurality of outlet connection channels 37b, the channel length L7 on the center side (vertex 36be side) of the outlet buffer portion 36b is greater than the channel length L8 on the end portion side (lower end side) of the outlet buffer portion 36b. Is also configured to be short (L7 <L8).

  As shown in FIG. 1, between the surface 16b of the anode-side separator 16 and the surface 14b of the cathode-side separator 14, cooling that communicates with the cooling medium inlet communication holes 22a, 22a and the cooling medium outlet communication holes 22b, 22b. A medium flow path 38 is formed. The cooling medium flow path 38 circulates the cooling medium over the electrode range of the electrolyte membrane / electrode structure 12, and the inlet buffer section 40a and the outlet buffer are provided in the vicinity of the inlet and the outlet of the cooling medium flow path 38, respectively. A portion 40b is provided.

  In the anode-side separator 16, the cooling medium flow path 38 has a back surface shape of the fuel gas flow path 34, and the inlet buffer portion 40a and the outlet buffer portion 40b have the back surface shapes of the outlet buffer portion 36b and the inlet buffer portion 36a. It is formed. In the cathode-side separator 14, the cooling medium flow path 38 has a back surface shape of the oxidant gas flow path 30, and the inlet buffer portion 40a and the outlet buffer portion 40b have back surface shapes of the inlet buffer portion 32a and the outlet buffer portion 32b. Formed as.

  A plurality of inlet connection channels 41a are provided in the vicinity of the cooling medium inlet communication hole 22a, and a plurality of outlet connection channels 41b are provided in the vicinity of the cooling medium outlet communication hole 22b.

  A first seal member 42 is integrally formed on the surfaces 14 a and 14 b of the cathode side separator 14 around the outer peripheral edge of the cathode side separator 14. A second seal member 44 is integrally formed on the surfaces 16 a and 16 b of the anode separator 16 so as to go around the outer peripheral edge of the anode separator 16. As the first seal member 42 and the second seal member 44, for example, EPDM, NBR, fluororubber, silicone rubber, fluorosilicone rubber, butyl rubber, natural rubber, styrene rubber, chloroprene or acrylic rubber or the like, cushion material Alternatively, an elastic seal member such as a packing material is used.

  The operation of the fuel cell 11 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 to the oxidant gas inlet communication hole 18a, and a fuel gas such as a hydrogen-containing gas is supplied to the fuel gas inlet communication hole 20a. Supplied. Further, a cooling medium such as pure water, ethylene glycol, or oil is supplied to the pair of cooling medium inlet communication holes 22a.

  Therefore, as shown in FIGS. 1 and 3, the oxidant gas passes from the oxidant gas inlet communication hole 18a through the inlet connection flow path 33a and the inlet buffer portion 32a to the oxidant gas flow path 30 of the cathode side separator 14. To be introduced. The oxidant gas moves in the arrow B direction (horizontal direction) along the oxidant gas flow path 30 and is supplied to the cathode electrode 26 of the electrolyte membrane / electrode structure 12.

  On the other hand, as shown in FIG. 4, the fuel gas is supplied from the fuel gas inlet communication hole 20a to the fuel gas passage 34 of the anode-side separator 16 through the inlet connection passage 37a and the inlet buffer portion 36a. The fuel gas moves in the horizontal direction (arrow B direction) along the fuel gas flow path 34 and is supplied to the anode electrode 28 of the electrolyte membrane / electrode structure 12 (see FIG. 1).

  Therefore, in the electrolyte membrane / electrode structure 12, the oxidant gas supplied to the cathode electrode 26 and the fuel gas supplied to the anode electrode 28 are consumed by an electrochemical reaction in the electrode catalyst layer to generate power. Is called.

  Next, as shown in FIGS. 1 and 3, the oxidant gas supplied to the cathode electrode 26 of the electrolyte membrane / electrode structure 12 is discharged from the outlet buffer portion 32b and the outlet connection channel 33b. The ink is discharged in the direction of arrow A along the communication hole 18b. On the other hand, as shown in FIG. 4, the fuel gas supplied to and consumed by the anode electrode 28 of the electrolyte membrane / electrode structure 12 passes along the fuel gas outlet communication hole 20b from the outlet buffer portion 36b and the outlet connection passage 37b. And discharged in the direction of arrow A.

  The cooling medium supplied to the pair of cooling medium inlet communication holes 22 a is introduced into the cooling medium flow path 38 between the cathode side separator 14 and the anode side separator 16. As shown in FIG. 1, the cooling medium once flows in the direction of arrow C (gravity direction) and then moves in the direction of arrow B (horizontal direction) to cool the electrolyte membrane / electrode structure 12. This cooling medium moves outward in the direction of arrow C, and is then discharged to the pair of cooling medium outlet communication holes 22b.

  In this case, in the first embodiment, as shown in FIG. 3, on the oxidant gas flow path 30 side, the plurality of inlet connection flow paths 33a are arranged on the central side (vertex 32ae side) of the inlet buffer portion 32a. The path length L1 is configured to be shorter than the flow path length L2 on the end side (upper end side) of the inlet buffer portion 32a (L1 <L2).

  Here, the plurality of inlet connection flow paths 33a are supplied to the oxidant gas flow path 30 using the structure (conventional example) in which the flow path lengths are set to the same length and the present application structure (example of the present application). The distribution of oxidant gas was compared. As a result, as shown in FIG. 5, in the structure of the conventional example, a large amount of oxidant gas flows from the oxidant gas inlet communication hole 18a to the end part side (upper end side) of the inlet buffer part 32a. The amount of oxidant gas flowing through the center of the portion 32a is small.

  Therefore, a large amount of oxidant gas is supplied to the upper end side in the width direction of the oxidant gas flow path 30 (near the oxidant gas inlet communication hole 18a), and a small amount of oxidant is supplied from the central part to the lower part of the power generation unit. Only gas is supplied. Therefore, there is a problem that the oxidant gas is supplied unevenly in the power generation unit, and durability and power generation stability are deteriorated.

  On the other hand, in the example of the present application, the pressure loss on the lower end side, which is the center side of the inlet buffer portion 32a, in the plurality of inlet connection channels 33a is the pressure loss on the upper end side, which is the end portion side of the inlet buffer portion 32a. It is comprised so that it may become smaller. Therefore, as shown in FIG. 6, the flow rate of the oxidant gas supplied from the center side to the lower side of the inlet buffer portion 32a is higher than the flow rate of the oxidant gas supplied to the upper end side of the inlet buffer portion 32a. Become large.

  Therefore, the oxidant gas can be supplied uniformly and reliably over the entire surface of the oxidant gas flow path 30 with a simple and economical configuration, and the desired power generation performance can be ensured. can get.

  The oxidant gas outlet communication hole 18b side is configured in the same manner as the oxidant gas inlet communication hole 18a, and the same effect can be obtained. Further, as shown in FIG. 4, the fuel gas flow channel 34 is configured in the same manner as the oxidant gas flow channel 30, and the same effects as those on the oxidant gas flow channel 30 side can be obtained.

  Further, in the first embodiment, a fuel constituted by a single electrolyte membrane / electrode structure 12, that is, a single MEA, and a cathode separator 14 and an anode separator 16, that is, two separators. Although the battery 11 is used, it is not limited to this. For example, a unit cell constituted by two MEAs and three separators (MEA interposed between separators) may be provided and applied to a cooling medium flow path constituted between the unit cells.

  FIG. 7 is an explanatory front view of the cathode-side separator 60 constituting the fuel cell stack according to the second embodiment of the present invention. The same components as those of the cathode separator 14 constituting the fuel cell stack 10 according to the first embodiment are denoted by the same reference numerals, and detailed description thereof is omitted.

  In the second embodiment, the oxidant gas inlet communication hole 18a and the fuel gas outlet communication hole 20b have a substantially rectangular shape and have substantially the same opening area. The oxidant gas outlet communication hole 18b and the fuel gas inlet communication hole 20a have a substantially rectangular shape and have substantially the same opening area.

  The cathode separator 60 is provided with an inlet buffer portion 62 a and an outlet buffer portion 62 b each having a plurality of protruding embosses in the vicinity of the inlet and outlet of the oxidant gas flow path 30. The inlet buffer 62a has a triangular shape along the shapes of the oxidant gas inlet communication hole 18a and the fuel gas outlet communication hole 20b. The first ridge line 62ar1 facing the oxidant gas inlet communication hole 18a and the second ridge line 62ar2 facing the fuel gas outlet communication hole 20b are set to the same length.

  The outlet buffer 62b has a triangular shape along the shapes of the oxidant gas outlet communication hole 18b and the fuel gas inlet communication hole 20a. The first ridge line 62br1 facing the oxidant gas outlet communication hole 18b and the second ridge line 62br2 facing the fuel gas inlet communication hole 20a are set to the same length.

  The plurality of inlet connection flow paths 33a have a flow path length L1 on the center side (vertex 62ae side) of the inlet buffer section 62a that is greater than a flow path length L2 on the end section side (upper end side) of the inlet buffer section 62a. Is also configured to be short (L1 <L2). In the plurality of outlet connection channels 33b, the channel length L3 on the center side (vertex 62be side) of the outlet buffer portion 62b is greater than the channel length L4 on the end side (lower end side) of the outlet buffer portion 32b. Is also configured to be short (L3 <L4). Although not shown, the fuel gas channel side is configured in the same manner as the oxidant gas channel 30 side.

  In the second embodiment configured as described above, the flow rate of the oxidant gas supplied from the center side to the lower side of the inlet buffer 62a is the same as that of the oxidant gas supplied to the upper end side of the inlet buffer 62a. Larger than the flow rate.

  As a result, the oxidant gas can be supplied uniformly and reliably over the entire surface of the oxidant gas flow path 30 with a simple and economical configuration, and the desired power generation performance can be ensured. The same effects as those of the first embodiment can be obtained.

  Further, in the present invention, the plurality of inlet connection flow paths 33a change the flow path width or flow path depth so that the pressure loss on the center side of the inlet buffer section 32a is reduced to the end side of the inlet buffer section 32a. Can be set smaller than the pressure loss. Similarly, the plurality of outlet connection channels 33b change the channel width or channel depth so that the pressure loss on the center side of the outlet buffer unit 32b is less than the pressure loss on the end side of the outlet buffer unit 32b. Can also be set small.

DESCRIPTION OF SYMBOLS 10 ... Fuel cell stack 11 ... Fuel cell 12 ... Electrolyte membrane and electrode structure 14, 60 ... Cathode side separator 16 ... Anode side separator 18a ... Oxidant gas inlet communication hole 18aw, 18bw, 20aw, 20bw ... Wall surface 18b ... Oxidant Gas outlet communication hole 20a ... Fuel gas inlet communication hole 20b ... Fuel gas outlet communication hole 22a ... Cooling medium inlet communication hole 22b ... Cooling medium outlet communication hole 24 ... Solid polymer electrolyte membrane 26 ... Cathode electrode 28 ... Anode electrode 30 ... Oxidation Agent gas flow paths 32a, 36a, 40a, 62a ... inlet buffer portions 32ae, 32be, 36ae, 36be ... apexes 32ar1, 32ar2, 32br1, 32br2, 36ar1, 36ar2, 36br1, 36br2, 62ar1, 62ar2, 62br1, 62br2, ... ridgeline 32b 36b, 40 b, 62b: outlet buffer portions 33a, 37a ... inlet connection flow path 33b, 37b ... outlet connection flow path 34 ... fuel gas flow path 38 ... cooling medium flow path

Claims (5)

An electrolyte membrane / electrode structure provided with electrodes on both sides of the electrolyte membrane and a fuel cell in which a horizontally long separator is laminated, and one reaction of fuel gas or oxidant gas is provided on the short side of the separator. A first reaction gas communication hole through which gas flows in the separator stacking direction and a second reaction gas communication hole through which the other reaction gas of the fuel gas or the oxidant gas flows in the separator stacking direction are provided. A fuel cell stack in which a plurality of the fuel cells are stacked,
The separator formed with the reaction gas flow path for flowing the one reaction gas in the long side direction along the separator surface is connected to the inlet side of the reaction gas flow path and the outlet side of the reaction gas flow path, respectively. While providing a triangular buffer part, provided a plurality of connecting flow channels connecting the first reaction gas communication hole and the buffer part,
The plurality of connection channels are channels directly connected along the separator surface from the first reaction gas communication hole to the buffer unit, and the channel length on the center side of the buffer unit is A fuel cell stack, characterized in that the fuel cell stack is configured to be shorter than the flow path length on the end side of the buffer section. The fuel cell stack according to claim 1, wherein the wall surface of the buffer portion of the first reactant gas passage, to the triangular ridge opposite to the first reactant gas passage of the buffer portion, intersect with each other A fuel cell stack characterized by extending in a direction to perform. An electrolyte membrane / electrode structure provided with electrodes on both sides of the electrolyte membrane and a fuel cell in which a horizontally long separator is laminated, and one reaction of fuel gas or oxidant gas is provided on the short side of the separator. A first reaction gas communication hole through which gas flows in the separator stacking direction and a second reaction gas communication hole through which the other reaction gas of the fuel gas or the oxidant gas flows in the separator stacking direction are provided. A fuel cell stack in which a plurality of the fuel cells are stacked,
The separator formed with the reaction gas flow path for flowing the one reaction gas in the long side direction along the separator surface is connected to the inlet side of the reaction gas flow path and the outlet side of the reaction gas flow path, respectively. While providing a triangular buffer part, provided a plurality of connecting flow channels connecting the first reaction gas communication hole and the buffer part,
The plurality of connection channels are channels directly connected along the separator surface from the first reaction gas communication hole to the buffer unit, and pressure loss on the center side of the buffer unit is caused by the buffer unit. The fuel cell stack is set to be smaller than the pressure loss on the end side of the fuel cell. 4. The fuel cell stack according to claim 1, wherein the first reaction gas communication hole is formed in a substantially rectangular shape that is inclined with respect to a triangular ridge line facing the first reaction gas communication hole of the buffer portion. A fuel cell stack characterized by comprising: 5. The fuel cell stack according to claim 1, wherein the first reaction gas communication hole and the second reaction gas communication hole both have a substantially rectangular shape and have substantially the same opening area. A fuel cell stack comprising:

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