TWM543472U - Bipolar plate gas-intake structure of fuel cell with drainage groove - Google Patents

Description

Fuel cell bipolar plate intake structure with drainage groove

The present invention relates to a fuel cell bipolar plate inlet structure with a drainage groove, in particular to a metal bipolar plate structure suitable for a fuel cell, which can effectively make fuel gas, oxidant, and coolant in the fuel cell. It is evenly distributed on a specific gas flow channel surface, and is further equipped with an innovative design seal to completely seal the gap between the fuel cells, avoid leakage of fuel gas and oxidant, and improve seal integrity to enhance the metal bipolar plate. Corrosion resistance, mechanical strength, and the life of the fuel cell.

According to the traditional petrochemical energy has been exhausted, and the use of petrochemical energy is likely to have a major impact on the ecological environment, the development of low-pollution and high-efficiency energy use has become the most important issue for governments; Among the various new energy utilization methods that have been developed, solar cells, biochemical energy sources, and fuel cells are more common. Among them, about 60% of fuel cells have high power generation efficiency and low pollution, which makes them attract attention. The fuel cell system is A power generation device that directly converts chemical energy into electrical energy. The fuel used may be methanol, ethanol, hydrogen or other hydrocarbons, and oxygen is used as an oxidant to generate electrical energy, which is generated during the electrochemical reaction. Water is a by-product of the reaction; compared with the conventional power generation method, the fuel cell has the advantages of low pollution, low noise, and high energy conversion efficiency, and since the fuel cell is directly generated by the oxidation of the fuel, the discharge current can be supplied with the fuel. The amount increases and increases, and as long as the fuel and oxygen are continuously supplied, the power generation will continue. No power failure and charging problems, and become very forward-looking and clean energy.

Basically, the fuel cell is mainly composed of a Membrane Electrode Assembly (MEA) and an electrode plate. The film electrode group is the core of the fuel cell, and functions as an electrochemical reaction, and the electrode plate affects the fuel cell business. One of the key factors of the electrode plate, the material of the electrode plate, the flow field structure or the processing cost, etc., have many problems to be solved; the conventional electrode plate materials mainly include graphite, composite carbon and metal substrates, for graphite and composite carbon materials. Although the formed electrode plate has the advantages of electrical conductivity and corrosion resistance, the process is complicated and time-consuming, and the thickness of the electrode plate made of the materials cannot be less than 3 mm, which is disadvantageous for the micro-fuel cell. For the electrode plate formed by the metal substrate, although the thickness is thin and the quality is light, the volume and quality of the fuel cell can be reduced. However, since the fuel of the fuel cell is transported through the flow path of the electrode plate, Therefore, the transport capacity of the flow channel directly affects the power generation efficiency of the fuel cell.

However, since the fuel and oxidant used in the fuel cell are gaseous forms of hydrogen and oxygen, and the coolant is in a liquid state, when the fuel, the oxidant, and the coolant are in the anode electrode plate and the cathode electrode plate, etc. When the flow path of the plates flows, a seal must be used to seal the gap between the membrane electrode set and the two bipolar plates to avoid leakage of fuel, oxidant, and coolant.

In addition, the conventional anode electrode plate or cathode electrode plate is designed to directly communicate with the gas inlet and outlet. Therefore, when assembling with a conventional sealing member, the inlet and outlet end portions must be additionally affixed with a metal piece as a reinforcement to enable The pressure generated by the combination of the anode and the cathode electrode plate avoids the risk of damage. However, this method complicates the assembly process and increases the chance of poor assembly and leakage. Therefore, the conventional seal is reduced in combination. The lack of the above is the direction in which the current bipolar plate structure of the fuel cell is to be improved.

Nowadays, the creators have many shortcomings in the actual implementation and application of the above-mentioned traditional seals. Therefore, they are a tireless spirit and are supplemented by their rich professional knowledge and years of practical experience. Improve, and based on this, create this creation.

The main purpose of the present invention is to provide a fuel cell bipolar plate inlet structure with a drainage groove, in particular to a gasket structure for sealing a bipolar plate such as an anode electrode plate and a cathode electrode plate of a fuel cell, and effectively filling the film. The gap between the electrode group and the bipolar plates such as the anode electrode plate and the cathode electrode plate can avoid the leakage of the fuel gas and the oxidant, and ensure the stability of the position of the film electrode group.

In order to achieve the above-mentioned implementation, the present inventors propose a fuel cell bipolar plate air intake structure having a drainage groove, which comprises at least one anode electrode plate and a cathode electrode plate; the anode electrode plate has a gas formed by press forming. a flow path surface and a first inlet portion and a first outlet portion disposed at two side ends of the gas flow passage surface, wherein the first inlet portion is perpendicular to the first outlet portion in a mirror-reversal symmetry; the gas flow passage surface has a plurality of streams The passage is for hydrogen flow, wherein the hydrogen gas enters from the hydrogen inlet end of the first inlet portion, flows into the flow passage via a hydrogen intake manifold, and is discharged to the hydrogen outlet of the first outlet portion via a hydrogen exhaust manifold. The first inlet portion is also provided with a coolant entering the manifold and an oxygen inlet end; the first outlet portion is also provided with a coolant outflow channel and an oxygen outlet end; and the cathode electrode plate is formed by stamping. a gas flow passage surface and a second inlet portion and a second outlet portion disposed at two side ends of the gas flow passage surface; the gas flow passage surface has a plurality of flow passages for oxygen flow, wherein the oxygen Entering from one of the oxygen inlet ends of the second inlet portion and flowing into the flow channel via an oxygen intake manifold, and then exhausting through an oxygen exhaust manifold to one of the oxygen outlet ends of the second outlet portion; wherein the second inlet portion is also a coolant inlet channel and a hydrogen inlet port are provided; the second outlet portion is also provided with a coolant outflow channel and an oxygen outlet port; and a first sealing member having a first sealing structure composed of three compartments And correspondingly disposed on the anode electrode plate, and the first sealing structure separates the first inlet portion, the first outlet portion, and the gas flow passage surface of the anode electrode plate from each other, and the first inlet portion overlaps with the first inlet portion a drainage groove for providing drainage hydrogen; and a second sealing member having a second sealing structure composed of three compartments, and correspondingly disposed on the cathode electrode plate, and the second sealing structure is a cathode electrode plate The second inlet portion, the second outlet portion, and the gas flow passage surface are isolated from each other, and the first inlet portion is formed to overlap with the second inlet portion to provide drainage oxygen.

In the fuel cell bipolar plate inlet structure with a drainage groove as described above, the material of the first sealing member is selected from the group consisting of Teflon or injection molded resin material.

The fuel cell bipolar plate inlet structure having a drainage groove as described above, the thickness of the first sealing member being between 0.4 mm and 0.8 mm.

The fuel cell bipolar plate inlet structure having a drainage groove as described above, and the material of the second sealing member is selected from the group consisting of Teflon or injection molded resin material.

The fuel cell bipolar plate inlet structure having a drainage groove as described above, the thickness of the second sealing member being between 0.4 mm and 0.8 mm.

The fuel cell bipolar plate inlet structure with the drainage groove as described above, the anode electrode plate and the cathode electrode plate are welded to the flow field to seal.

The fuel cell bipolar plate intake structure with a drainage groove as described above is welded by laser welding.

The present invention further provides a fuel cell, which is a pair of bipolar plates and a first sealing member welded according to an anode electrode plate and a cathode electrode plate in the fuel cell bipolar plate structure of the above-mentioned optimized sealing member. And a second sealing member is respectively disposed on the two side ends of the conventional membrane electrode assembly (MEA), the two sets of bipolar plates are oppositely disposed oppositely, and the arrangement between the bipolar plates is sequentially the first sealing member and the thin film electrode. The group and the second seal are formed to form a fuel cell unit, and a plurality of fuel cell units are connected in series to form a fuel cell.

In the fuel cell as described above, the first sealing member is disposed at one end of the anode electrode plate of the bipolar plate, and the second sealing member is disposed at one end of the cathode electrode plate of the bipolar plate.

Therefore, the fuel cell bipolar plate air intake structure of the present invention has a first sealing member which is disposed on the anode electrode plate and the cathode electrode and is formed by cutting a Teflon sheet or injection molding a resin material. And a second sealing member to fill the gap between the membrane electrode assembly and the anode and cathode metal bipolar plates to avoid leakage of fuel gas and oxidant, and to ensure the stability of the position of the membrane electrode assembly; in addition, the creation of the optimized sealing member The fuel cell bipolar plate structure directly uses the laser welding method to achieve the sealing of the flow field, and the anode and cathode metal bipolar plates are joined to the outer ring contact surface as the welding place, when the gas inlet and outlet and the two metal double When the outer frame bead is completed, the sealing purpose can be achieved, the leakage of the cooling liquid can be avoided, and the support can be strengthened to strengthen the overall battery structure.

The purpose of this creation and the advantages of its structural design function will be explained in accordance with the preferred embodiment shown in the following figures, so that the reviewing committee can have a deeper and more specific understanding of the creation.

First, referring to the first and second figures, a top view of a structure of an anode electrode plate of a preferred embodiment of a fuel cell bipolar plate inlet structure having a drainage groove, and a top view of a cathode electrode plate structure, wherein The fuel cell bipolar plate structure with optimized seals is at least included:

An anode electrode plate (1) having a gas flow path surface (11) formed by press working and a first inlet portion (12) and a first outlet portion (13) disposed at both side ends of the gas flow path surface (11) Wherein the first inlet portion (12) is quadri-mirror-inverted symmetrically with the first outlet portion (13); the gas flow channel surface (11) has a plurality of flow channels (111) for hydrogen flow, wherein the hydrogen gas is A hydrogen inlet end (121) of the first inlet portion (12) enters and flows into the flow channel (111) via a hydrogen intake manifold (112), and is discharged to the first through a hydrogen exhaust manifold (113). a hydrogen outlet end (131) of the outlet portion (13); wherein the first inlet portion (12) is also provided with a coolant inlet manifold (122) and an oxygen inlet port (123); the first outlet portion (13) The system also has a coolant outflow channel (132) and an oxygen outlet end (133); in addition, the anode electrode plate (1) is made of a metal material, and the best metal material is a stainless steel plate, and the thickness of the plate is Between 0.1mm~0.2mm, the best system is 0.15mm, and the total area of the anode electrode plate (1) is 202.7cm ² , the flow channel elongation is 0.5mm, and the flow channel width is 1mm. Reaction area 132cm ^2;

A cathode electrode plate (2) has a gas flow path surface (21) formed by press working and a second inlet portion (22) and a second outlet portion (23) disposed at both side ends of the gas flow path surface (21). Wherein the second inlet portion (22) is quadri-mirror-inverted symmetrically with the second outlet portion (23); the gas flow passage surface (21) has a plurality of flow passages (211) for oxygen flow, wherein the oxygen is An oxygen inlet end (223) of the second inlet portion (22) enters and flows into the flow passage via an oxygen intake manifold (212), and is discharged to the second outlet portion via an oxygen exhaust manifold (213). An oxygen outlet end (233); wherein the second inlet portion (22) is also provided with a coolant inlet manifold (222) and a hydrogen inlet port (221); the second outlet portion (23) is also provided with a The coolant flows out of the manifold (232) and an oxygen outlet end (233); in addition, the cathode electrode plate (2) is made of a metal material, and the best metal material is a stainless steel plate, and the thickness of the plate is 0.1 mm. Between ~0.2mm, the optimum system is 0.15mm, and the total area of the cathode electrode plate (2) is 202.7cm ² , the flow channel elongation is 0.5mm, the flow channel width is 1mm, and the total reaction area is 132 Cm ² ;

a first sealing member (14) having a first sealing structure (141) composed of three compartments, and correspondingly disposed on the anode electrode plate (1), and the first sealing structure (141) is an anode electrode plate (1) The first inlet portion (12), the first outlet portion (13), and the gas flow passage surface (11) are isolated from each other, and the first inlet portion (12) overlaps with the first inlet portion (12) to form a first drainage recess a groove (124) for allowing external hydrogen to be introduced; further, the material of the first sealing member (14) is selected from one of Teflon or injection molded resin material; and further, the first sealing member (14) The thickness of the first sealing member (14) is formed by injection molding of a resin material in a preferred embodiment of the present invention to facilitate subsequent mass production. Required, and the thickness of the first seal (14) is designed to be 0.6 mm;

a second sealing member (24) having a second sealing structure (241) composed of three compartments, and correspondingly disposed on the cathode electrode plate (2), and the second sealing structure (241) is a cathode electrode plate (2) The second inlet portion (22), the second outlet portion (23), and the gas flow passage surface (21) are separated from each other, and the second inlet portion (22) overlaps with the second inlet portion (22) to form a second drainage concave The groove (224) enables external oxygen to be introduced; further, the material of the second sealing member (24) is selected from one of Teflon or injection molded resin materials; and, in addition, the second sealing member (24) The thickness of the second sealing member (24) is formed by injection molding the resin material in a preferred embodiment of the present invention, so as to facilitate subsequent mass production. Required, and the thickness of the second seal (24) is designed to be 0.6 mm.

In addition, the anode electrode plate (1), the cathode electrode plate (2) or the coolant flow channel portion is welded to the flow field to seal, and the best is achieved by laser welding, the anode electrode plate (1) and The contact surface of the outer electrode of the cathode electrode plate (2) is a welded portion. When the gas inlet and outlet and the outer frame bead of the two metal bipolar plates are completed, the sealing purpose can be achieved, the leakage of the cooling liquid is avoided, and the support is strengthened to strengthen the whole. The role of the battery structure, so its welding quality is critical, the advantages of using laser welding are revealed.

Furthermore, please refer to the third figure, which is a schematic diagram of a fuel cell unit stacking of a preferred embodiment of a fuel cell bipolar plate inlet structure with a drainage groove, wherein the present invention further provides a fuel cell. The fuel cell is formed by a plurality of fuel cell units (3), wherein the fuel cell unit (3) comprises a conventional membrane electrode assembly (31), an anode electrode plate (1) and a cathode electrode. The plate (2) is welded with two sets of bipolar plates (32), a first sealing member (14), and a second sealing member (24), and the two sets of bipolar plates (32) are reversely oppositely disposed, bipolar The arrangement between the plates (32) is a first sealing member (14), a membrane electrode assembly (31) and a second sealing member (24); in addition, the first sealing member (14) is disposed on the bipolar plate (32). One end of the anode electrode plate (1), and the second sealing member (24) is disposed at one end of the cathode electrode plate (2) of the bipolar plate (32).

Please refer to the fourth figure again for a schematic diagram of a drainage groove of a preferred embodiment of the fuel cell bipolar plate inlet structure with a drainage groove, wherein the anode electrode plate (1) and the cathode are shown. When the electrode plates (2) are reversely overlapped, the hydrogen of the fuel gas enters from the hydrogen inlet ends (121, 221), and enters the anode electrode through the gap between the hydrogen inlet channels and the cathode electrode plates (2) below. The gas flow path (11) of the plate (1), the path indicated by the black arrow in the fourth figure, is the route traveled by the hydrogen gas of the fuel gas.

Furthermore, as shown in the fifth figure, a cross-sectional view of a fuel cell unit of a preferred embodiment of the fuel cell bipolar plate inlet structure with a drainage groove is created, which is an oxygen inlet end (123, 223). a bipolar plate (32) in which the anode electrode plate (1) and the cathode electrode plate (2) are overlapped, wherein an arrow in the flow path (111, 211) through which the gas flows is indicative of oxygen entering from the inlet end. The rear flow direction, while the first seal (14) and the second seal (24) are completely sealed to prevent gas leakage.

According to the fuel cell bipolar plate inlet structure with the above-mentioned drainage groove, in practice, first, the anode electrode plate (1) and the cathode electrode plate (2) of the present invention are made of metal material, and the best metal is used. The material is stainless steel, the thickness of the stainless steel plate is between 0.1mm~0.2mm, the best is 0.15mm, the total area is 202.7cm ² , the flow channel is 0.5mm, and the flow channel width is The total reaction area is 132 cm ² , and the processing method is to press out the desired gas flow path by press forming; wherein the anode electrode plate (1) has a gas flow path surface (11) formed by press working and a first inlet portion (12) and a first outlet portion (13) disposed at two side ends of the gas flow passage surface (11), wherein the first inlet portion (12) and the first outlet portion (13) are twice mirrored The gas flow channel surface (11) has a plurality of flow channels (111) for hydrogen gas flow, wherein the hydrogen gas is introduced by a hydrogen inlet end (121) of the first inlet portion (12) and is introduced through a hydrogen gas inlet. After the manifold (112) flows into the flow channel (111), it is discharged to a hydrogen outlet end of the first outlet portion (13) via a hydrogen exhaust manifold (113) (1) 31) wherein the first inlet portion (12) is also provided with a coolant inlet manifold (122) and an oxygen inlet port (123); the first outlet portion (13) is also provided with a coolant outflow channel (132). And an oxygen outlet end (133); further, the cathode electrode plate (2) has a gas flow path surface (21) formed by press working and a second inlet disposed at two side ends of the gas flow path surface (21) a portion (22) and a second outlet portion (23), wherein the second inlet portion (22) and the second outlet portion (23) are quadrilaterally mirror-inverted symmetrical; the gas flow passage surface (21) has a plurality of flow passages ( 211) for supplying oxygen, wherein oxygen is introduced from one of the oxygen inlet ends (223) of the second inlet portion (22), and flows into the flow passage via an oxygen intake manifold (212), and then passes through an oxygen exhaust manifold. (213) discharged to one of the second outlet portion (23) of the oxygen outlet end (233); wherein the second inlet portion (22) is also provided with a coolant inlet manifold (222) and a hydrogen inlet end (221); The second outlet portion (23) is also provided with a coolant outflow channel (232) and an oxygen outlet end (233);

The first sealing member (14) has a first sealing structure (141) composed of three compartments, and is correspondingly disposed on the anode electrode plate (1), and the first sealing structure (141) is an anode electrode plate. (1) The first inlet portion (12), the first outlet portion (13), and the gas flow passage surface (11) are isolated from each other, and the first inlet portion (12) overlaps with the first inlet portion (12) to form a first drainage recess a groove (124) for allowing external hydrogen to be introduced; wherein the material of the first sealing member (14) is formed by injection molding a resin material to facilitate subsequent mass production, and the first sealing member (14) The thickness is designed to be 0.6 mm; further, the second sealing member (24) has a second sealing structure (241) composed of three compartments, and is correspondingly disposed on the cathode electrode plate (2), and second The sealing structure (241) isolates the second inlet portion (22), the second outlet portion (23), and the gas flow passage surface (21) of the cathode electrode plate (2) from each other, and the second inlet portion (22) The overlapping portion may form a second drainage groove (224) to allow external oxygen to be introduced; wherein the material of the second sealing member (24) is formed by injection molding the resin material to facilitate The need for mass production continues, while the thickness of the second seal (24) is designed to be 0.6 mm. The first sealing member (14) and the second sealing member (24) must be slightly thicker than the thin film electrode assembly (MEA) to withstand the deformation of the packaging pressure, and can effectively reach the sealed state.

Finally, the practical application of the fuel cell is to connect a plurality of fuel cell units (3) in series to form a fuel cell to obtain sufficient power generation. In the fuel cell unit (3), an anode electrode plate (1) and A cathode electrode plate (2) is welded into a bipolar plate (32), and the gas flow path surface (11) of the anode electrode plate (1) and the gas flow path surface (21) of the cathode electrode plate (2) are bonded to each other. A plurality of vacancies are formed by staggering, and the vacancy forms a coolant flow path through which the coolant flows, that is, a gas flow path surface of the gas flow path (11) and the cathode electrode plate (2) of the anode electrode plate (1) ( The back side of 21), that is, the outer side of the anode electrode plate (1) and the cathode electrode plate (2), when the outer sides of the anode electrode plate (1) and the cathode electrode plate (2) overlap each other, the electrode plate is in contact with the electrode plate The place will create a barrier, and the non-contact vacancy will produce a liquid flow that provides a coolant for the passage, which is a so-called coolant flow path, and a grid shape produced by laminating the anode electrode plate (1) and the cathode electrode plate (2) Space can be used as a passage for coolant circulation, and the coolant flow field is expected to reach the largest possible area. The cooling effect and the contact point must also be enough to withstand the pressure of the fuel cell compression assembly. Therefore, the metal bipolar plate system such as the anode electrode plate (1) and the cathode electrode plate (2) has a flexible and delicate design, which can simultaneously satisfy Cooling demand and providing higher weight and power density; further, preparing a fuel cell unit (3), taking two sets of bonded bipolar plates (32), a first sealing member (14), and a second a sealing member (24), the two sets of bipolar plates (32) are oppositely arranged oppositely, and the arrangement between the bipolar plates (32) is a first sealing member (14), a thin film electrode group (31) and a second sealing. Further, the first sealing member (14) is disposed at one end of the anode electrode plate (1) of the bipolar plate (32), and the second sealing member (24) is disposed on the bipolar plate (32) One end of the cathode electrode plate (2), and a plurality of fuel cell units (3) connected in series to form a fuel cell; wherein the first sealing member (14) and the second sealing member (24) must be laminated after the film The electrode group (31) (MEA) is slightly thick to withstand the deformation of the package pressure, and can effectively achieve the sealed state, and the first sealing member (14) and the second sealing member (24) can be completely dense. The gap between the fuel cells avoids leakage of fuel gas and oxidant to improve the integrity of the seal; and the first seal (14) and the second seal (24) can be combined with the bipolar plate (32) in addition to improving the integrity of the seal. In time, the corresponding first inlet portion (12) or second inlet portion (22) forms a first drainage groove (124) and a second drainage groove (224), so that external gas can be introduced into the reaction. .

It can be seen from the above description that the fuel cell bipolar plate air intake structure with the drainage groove is compared with the prior art, and the creation has the following advantages:

1. The fuel cell bipolar plate air intake structure of the present invention has a first sealing member which is formed on the anode electrode plate and the cathode electrode and is formed by cutting a Teflon sheet or injection molding a resin material. The second sealing member fills the gap between the membrane electrode assembly and the anode and cathode metal bipolar plates to avoid leakage of fuel gas and oxidant, and ensures the stability of the position of the membrane electrode assembly, compared with the conventional sealing assembly. The outlet end must be additionally affixed with a metal sheet as a reinforcement to make the assembly process more complicated, and it will increase the chance of poor assembly and leakage. This creation system can simplify the assembly process and improve the sealing integrity and achieve good mechanical strength. Can improve the life of fuel cells.

2. The first sealing member or the second inlet portion of the fuel cell bipolar plate air intake structure of the present invention having a drainage groove and the second sealing member and the second sealing plate are overlapped with the bipolar plate A drain groove is formed to provide an inflow of gas, replacing the portion of the previous gas flow path that is in direct communication with the gas inlet and outlet, and, in contrast, reduces the likelihood of leakage.

3. The fuel cell bipolar plate air intake structure with drainage groove of the present invention directly uses the laser welding method to achieve the sealing of the flow field, and the anode and cathode metal bipolar plates are in contact with the outer ring. When the surface is welded, when the gas inlet and outlet and the two metal bipolar outer frame bead are completed, the sealing purpose can be achieved, the leakage of the cooling liquid can be avoided, and the support can be strengthened to strengthen the overall battery structure.

In summary, the fuel cell bipolar plate air intake structure with drainage grooves can achieve the intended use efficiency by the above disclosed embodiments, and the creation has not been disclosed before the application. It has fully complied with the requirements and requirements of the Patent Law. If you apply for a new type of patent in accordance with the law, you are welcome to review it and grant a patent.

However, the illustrations and descriptions disclosed above are only preferred embodiments of the present invention, and are not intended to limit the scope of protection of the present invention; those who are familiar with the skill are otherwise characterized by the scope of the creation. Equivalent changes or modifications shall be considered as not departing from the design of this creation.

(1)‧‧‧Anode electrode plate
(11) ‧‧‧ gas flow surface

(111)‧‧‧ flow path
(112)‧‧‧ Hydrogen intake manifold

(113)‧‧‧ Hydrogen exhaust manifold
(12) ‧ ‧ first entrance

(121)‧‧‧ Hydrogen inlet end
(122) ‧‧‧ coolant entering the lane

(123)‧‧‧Oxygen inlet end
(124)‧‧‧First drainage groove

(13) ‧ ‧ First Export Department
(131)‧‧‧ Hydrogen outlet

(132) ‧‧‧ coolant outflow manifold
(133)‧‧‧Oxygen outlet

(14)‧‧‧First seal
(141)‧‧‧First sealing structure

(2) ‧‧‧cathode electrode plate
(21) ‧‧‧ gas flow surface

(211)‧‧‧Runner
(212) ‧‧‧Oxygen intake manifold

(213)‧‧‧Oxygen exhaust manifold
(22) ‧‧‧Second entrance

(221)‧‧‧ Hydrogen inlet end
(222) ‧‧‧ coolant entering the lane

(223)‧‧‧Oxygen inlet end
(224)‧‧‧Second drainage groove

(23) ‧ ‧ Second Export Department
(231) ‧‧‧ Hydrogen outlet

(232) ‧‧‧ coolant outflow manifold
(233) ‧‧‧Oxygen outlet

(24)‧‧‧Second seals
(241)‧‧‧Second sealing structure

(3)‧‧‧ fuel cell unit
(31) ‧‧‧Thin electrode group

(32)‧‧‧Bipolar plates

The first figure: a top view of an anode electrode plate structure of a preferred embodiment of a fuel cell bipolar plate inlet structure with a drainage groove

The second figure: a top view of a cathode electrode plate structure of a preferred embodiment of a fuel cell bipolar plate inlet structure with a drainage groove

The third figure: a schematic diagram of a fuel cell unit stacking of a preferred embodiment of a fuel cell bipolar plate inlet structure with a drainage groove

The fourth figure: a schematic diagram of a drainage groove of a preferred embodiment of a fuel cell bipolar plate inlet structure with a drainage groove

Fig. 5 is a cross-sectional view showing a fuel cell unit of a preferred embodiment of a fuel cell bipolar plate inlet structure with a drainage groove

(1)‧‧‧Anode electrode plate

(11) ‧‧‧ gas flow surface

(111)‧‧‧ flow path

(112)‧‧‧ Hydrogen intake manifold

(113)‧‧‧ Hydrogen exhaust manifold

(12) ‧ ‧ first entrance

(121)‧‧‧ Hydrogen inlet end

(122) ‧‧‧ coolant entering the lane

(123)‧‧‧Oxygen inlet end

(124)‧‧‧First drainage groove

(13) ‧ ‧ First Export Department

(131)‧‧‧ Hydrogen outlet

(132) ‧‧‧ coolant outflow manifold

(133)‧‧‧Oxygen outlet

(14)‧‧‧First seal

(141)‧‧‧First sealing structure

Claims (9)

A fuel cell bipolar plate air intake structure having a drainage groove includes at least: an anode electrode plate having a gas flow path surface formed by press working and a first side disposed at two side ends of the gas flow path surface An inlet portion and a first outlet portion, wherein the first inlet portion and the first outlet portion are quadri-mirror-versal symmetrical; the gas flow passage surface has a plurality of flow passages for hydrogen flow, wherein the hydrogen is a hydrogen inlet end of an inlet portion enters and flows into the channels through a hydrogen inlet manifold, and is discharged to a hydrogen outlet end of the first outlet portion via a hydrogen exhaust manifold; wherein the first inlet portion A coolant inlet channel and an oxygen inlet port are also provided; the first outlet portion is also provided with a coolant outflow channel and an oxygen outlet port; and a cathode electrode plate having a gas flow channel surface formed by press forming. And a second inlet portion and a second outlet portion disposed at two side ends of the gas flow passage surface, wherein the second inlet portion and the second outlet portion are quadrilaterally mirror-inverted symmetrical; the gas flow passage surface has a complex a flow path for oxygen to flow, wherein the oxygen enters from an oxygen inlet end of the second inlet portion and flows into the flow passage via an oxygen intake manifold, and is discharged to the first via an oxygen exhaust manifold An oxygen outlet end of the second outlet portion; wherein the second inlet portion is also provided with a coolant inlet passage and a hydrogen inlet end; the second outlet portion is also provided with a coolant outflow passage and an oxygen outlet end; The first sealing member has a first sealing structure composed of three compartments, and is correspondingly disposed on the anode electrode plate, and the first sealing structure is a first inlet portion and a first outlet portion of the anode electrode plate And the gas flow passage faces are isolated from each other, and the first inlet portion overlaps to form a first drainage groove to provide drainage of the hydrogen; and a second seal has a three compartment composition a sealing structure corresponding to the cathode electrode plate, and the second sealing structure isolating the second inlet portion, the second outlet portion, and the gas flow passage surface of the cathode electrode plate from each other, and the second inlet unit The overlap forms a second drainage groove to provide drainage of the oxygen. The fuel cell bipolar plate air intake structure with a drainage groove according to claim 1, wherein the material of the first sealing member is one selected from the group consisting of Teflon or injection molded resin materials. The fuel cell bipolar plate air intake structure with a drainage groove according to claim 2, wherein the first sealing member has a thickness of between 0.4 mm and 0.8 mm. The fuel cell bipolar plate air intake structure with a drainage groove according to claim 1, wherein the material of the second sealing member is one selected from the group consisting of Teflon or injection molded resin materials. The fuel cell bipolar plate air intake structure with a drainage groove according to claim 4, wherein the thickness of the second sealing member is between 0.4 mm and 0.8 mm. The fuel cell bipolar plate inlet structure with a drainage groove as described in claim 1, wherein the anode electrode plate and the cathode electrode plate are welded to each other to achieve a flow field seal. A fuel cell bipolar plate intake structure having a drainage groove as described in claim 6 wherein the welding method is laser welding. A fuel cell is composed of a plurality of fuel cell units, wherein the fuel cell unit comprises a conventional membrane electrode assembly, two sets of bipolar plates welded by an anode electrode plate and a cathode electrode plate, and a first a sealing member, and a second sealing member, the two sets of bipolar plates are oppositely disposed opposite to each other, and the arrangement between the bipolar plates is sequentially the first sealing member, the thin film electrode assembly and the second sealing member. The anode electrode plate, the cathode electrode plate, the first sealing member and the second sealing member are the fuel cell bipolar plate structure with an optimized sealing member according to any one of claims 1 to 7. The fuel cell of claim 8, wherein the first sealing member is disposed at one end of the anode electrode plate of the bipolar plate, and the second sealing member is disposed on the cathode electrode plate of the bipolar plate. One end.