WO2017181533A1 - Pem fuel cell stack, and flow field plate assembly for same - Google Patents

Pem fuel cell stack, and flow field plate assembly for same Download PDF

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Publication number
WO2017181533A1
WO2017181533A1 PCT/CN2016/088556 CN2016088556W WO2017181533A1 WO 2017181533 A1 WO2017181533 A1 WO 2017181533A1 CN 2016088556 W CN2016088556 W CN 2016088556W WO 2017181533 A1 WO2017181533 A1 WO 2017181533A1
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WO
WIPO (PCT)
Prior art keywords
flow field
field plate
plate
anode
cathode
Prior art date
Application number
PCT/CN2016/088556
Other languages
French (fr)
Chinese (zh)
Inventor
李骁
赵锋
Original Assignee
武汉众宇动力系统科技有限公司
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Publication date
Priority claimed from CN201620337978.1U external-priority patent/CN205828543U/en
Priority claimed from CN201610250337.7A external-priority patent/CN105870476B/en
Application filed by 武汉众宇动力系统科技有限公司 filed Critical 武汉众宇动力系统科技有限公司
Publication of WO2017181533A1 publication Critical patent/WO2017181533A1/en

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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0258Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Definitions

  • the present invention relates to the field of fuel cell technology, and more particularly to a polymer thin film battery stack for a proton exchange membrane (PEM) fuel cell.
  • PEM proton exchange membrane
  • a fuel cell is an energy source that converts chemical energy from a fuel into electrical energy through a chemical reaction involving a reactive species, such as oxygen or other oxidant. Hydrogen is the most common fuel in such batteries. Among them, the most representative example of such a fuel cell technology is a proton exchange membrane (PEM) fuel cell.
  • PEM proton exchange membrane
  • Such a fuel cell includes a membrane electrode assembly (MEA) including a polymer electrolyte membrane sandwiched between two layers of catalyst coated papers respectively as yin and yang grades; the membrane electrode assembly (MEA) is sandwiched between a pair of streams Between field plates, they are related to fuel and oxidant, respectively.
  • the working principle of the fuel cell comprises the steps of: passing hydrogen fuel into an anode flow field plate on one side of the fuel cell, and then passing the oxidant into a cathode flow field plate on the other side of the fuel cell; and a platinum catalyst (or other catalyst)
  • hydrogen is separated into positively charged hydrogen protons and negatively charged hydrogen electrons; the polymer electrolyte membrane can only pass positively charged hydrogen protons into the cathode, while negatively charged hydrogen electrons need to enter the cathode through the channels of the peripherals.
  • current is generated; on the cathode side, electrons and positively charged protons combine with oxygen to form water, which is the only product discharged from the battery.
  • oxygen since oxygen is blown into the cathode flow field plate, the fuel cell can be cooled.
  • the cathode flow field plate can be exposed to air as an "open cathode structure."
  • the traditional cathode flow field plate design uses a saw-like or square wave structure, and air can be blown into it by a blower or a fan. Compared to water-cooled cell stacks, air-cooled cell stacks have a more balanced design and easier control strategy that can be activated immediately.
  • the saw-like cathode flow field plate faces the membrane electrode assembly, which includes a polymer electrolyte membrane and catalyst layers on both sides. Therefore, only the serrations are pressed against the gasket, and other portions of the region are not subjected to the pressure of the serrations and are difficult to be sealed, so as to become potential hydrogen leakage regions.
  • the design generally defines a hydrogen working pressure of less than 0.5 bar.g. However, higher hydrogen pressures can promote kinetics, battery uniformity, load change response, and reduced hydrogen starvation (serious damage to fuel power) The durability of the pool), but higher than the design pressure value may cause leakage or gasket burst.
  • a primary object of the present invention is to provide a fuel cell in which a flow field plate set for a proton exchange membrane fuel cell is incorporated to prevent hydrogen leakage.
  • Another object of the present invention is to provide a flow field plate set that allows for higher fuel cell operating pressures and improved cooling efficiency. This performance increases the power-to-weight ratio and endurance of a fuel cell as a source of high energy density energy.
  • Another object of the present invention is to provide a flow field plate set in which the inner side of the cathode flow field plate of the flow field plate group and the inner side of the anode flow field plate form two continuous faces facing each other, thereby making the flow field plate
  • a seal between the inner side of the cathode flow field plate and the inner side of the anode flow field plate is achieved by providing only one sealing film between the inner side of the cathode flow field plate and the inner side of the anode flow field plate.
  • the single sealing film of the flow field plate group realizes the sealing between the inner side of the cathode flow field plate and the inner side of the anode flow field plate, so that the assembly difficulty of the flow field plate group is reduced.
  • Another object of the present invention is to provide a flow field plate set for a proton exchange membrane fuel cell to enable the proton exchange membrane fuel cell to operate at a pressure greater than 0.5 bar.g without hydrogen leakage and thus The operation is safer.
  • Another object of the present invention is to provide a flow field plate set for a proton exchange membrane fuel cell to enable the proton exchange membrane fuel cell to operate at a pressure greater than 0.5 bar.g, thereby allowing the fuel cell to be compared
  • the kinetics, battery uniformity, load change response are increased and the probability of hydrogen starvation is reduced.
  • Another object of the present invention is to provide a flow field plate set for a proton exchange membrane fuel cell to enhance air cooling efficiency, thereby allowing the use of a thinner flow field plate capable of reducing the total weight to power ratio.
  • Another object of the present invention is to provide a flow field plate set for a proton exchange membrane fuel cell to reduce the sensitivity of the water content of the proton exchange membrane to the fan speed.
  • Another object of the present invention is to provide a flow field plate set for a proton exchange membrane fuel cell wherein the newly designed flow field plate of the flow field plate set is easier to seal and prevent hydrogen leakage.
  • Another object of the present invention is to provide a flow field plate set for a proton exchange membrane fuel cell, wherein the newly designed flow field plate can be adapted for assembly in most conventional proton exchange membrane fuel cells.
  • Another object of the present invention is to provide a flow field plate set for a proton exchange membrane fuel cell wherein the newly designed flow field plate is easy to use, simple in construction, and inexpensive to manufacture.
  • a fuel cell including a membrane electrode assembly and a first-rate field plate assembly.
  • the flow field plate set includes a cathode flow field plate and an anode flow field plate, wherein the membrane electrode assembly is sealed between the cathode flow field plate and the anode flow field plate, wherein the cathode flow field plate has a planar side An opposite channel side and a plurality of fluid channels formed on the channel side, wherein the planar side is located outside of the cathode flow field plate toward the outside of the membrane electrode set, wherein the fluid channel is configured to enable fluid along the Fluid channels are directed to the set of membrane electrodes to facilitate electrochemical reaction to generate and generate electrical energy through the membrane electrode, wherein the anode flow field plate has a planar side, an opposite channel side, and at least one fuel passage, wherein the anode flow field
  • the planar side of the plate is located on an inner side of the anode flow field plate, the channel side of the anode flow field plate is located on an outer side of the anode flow field plate and seals the membrane electrode set, wherein each of the anode flow field plates
  • the present invention further provides a cathode flow field plate for a fuel cell, wherein the fuel cell has a membrane electrode set including a cathode flow field plate, wherein the cathode flow field plate is arranged to seal the membrane electrode
  • the set wherein the cathode flow field plate has a plurality of fluid passages and a set of cooling passages, wherein the cooling passages are respectively in communication with the fluid passages.
  • the present invention further provides an anode flow field plate for a fuel cell, wherein the fuel cell has a membrane electrode set including an anode flow field plate, wherein the anode flow field plate has a planar side and a channel a side, wherein the planar side is located on an inner side of the anode flow field plate, wherein the channel side is located on an outer side of the anode flow field plate, wherein the channel side of the anode flow field plate is configured to seal the membrane electrode set, wherein the anode flow field plate further includes at least one fuel passage, wherein the fuel passage is formed toward the passage side of the membrane electrode assembly such that fuel can be supplied to the membrane electrode assembly through the fuel passage.
  • the present invention still further provides a flow field plate set for a fuel cell, wherein the fuel cell has at least one membrane electrode set including at least two flow field plates, wherein the membrane electrode groups of the fuel cell are respectively disposed at Between two adjacent flow field plates, wherein each flow field plate comprises a cathode plate body, an anode plate body and a set of guide walls, wherein the cathode plate body forms a set of first fluid grooves spaced apart from each other, wherein The guiding wall is spaced apart between the cathode plate body and the anode plate body such that each adjacent two guiding walls form a second fluid groove between the two, wherein the cathode plate body The first fluid grooves are disposed to communicate with the second fluid grooves, respectively, such that each of the first fluid grooves and the corresponding second fluid grooves form at least one continuous fluid passage, wherein the fluid passage has a first passage opening a second passage opening and a third passage opening, wherein the anode plate body of the flow field plate has at least one set a
  • the present invention still further provides a fuel cell comprising at least one membrane electrode assembly and one flow field plate group, wherein the flow field plate group comprises at least two flow field plates, wherein the membrane electrode groups are respectively disposed adjacent to the two Between the flow field plates, wherein each flow field plate comprises a cathode plate body, an anode plate body and a set of guide walls, wherein the cathode plate body forms a set of spaced apart first fluid grooves, wherein the guide wall Separably disposed between the cathode plate body and the anode plate body such that each adjacent two guide walls form a second fluid groove therebetween, wherein the first portion of the cathode plate body
  • the fluid slots are disposed in communication with the second fluid channels, respectively, such that each of the first fluid channels and the respective second fluid grooves form at least one continuous fluid passage, wherein the fluid passage has a first passage opening, a first a two-channel opening and a third passage opening, wherein the anode plate body of the flow field plate has at least one fuel passage
  • the present invention still further provides a flow field plate set for a fuel cell, wherein the fuel cell has at least one membrane electrode set including at least two flow field plates, wherein the membrane electrode of the fuel cell
  • the groups are respectively disposed between two adjacent flow field plates, wherein each flow field plate includes a cathode plate body, an anode plate body and a set of guide walls, wherein the cathode plate body forms a set of mutually separated first a fluid groove, wherein the guide wall is spaced apart between the cathode plate body and the anode plate body such that each adjacent two guide walls form a second fluid groove between the two, wherein
  • the first fluid grooves of the cathode plate body are disposed to communicate with the second fluid grooves, respectively, such that each of the first fluid grooves and the corresponding second fluid grooves form at least one continuous fluid passage, wherein the fluid passage has a first passage opening, a second passage opening and a third passage opening, wherein the anode plate body of the flow field plate has at least one fuel
  • the present invention still further provides a fuel cell comprising at least one membrane electrode set and at least two flow field plates, wherein the membrane electrode sets are respectively disposed between adjacent two flow field plates, wherein each flow field plate
  • the invention comprises a flow field plate body, a set of first guiding walls and a set of second guiding walls, wherein the flow field plate body has a cathode side and an anode side, wherein the flow field plate body has at least one disposed at the anode a side fuel passage, wherein the first guide wall is spaced apart from the cathode side of the flow field plate, the second guide wall respectively extending from the first guide wall, so that two adjacent first The guiding wall forms a first fluid passage between the two, and the corresponding adjacent two second guiding walls form a second fluid passage therebetween, wherein the first fluid passage and the second fluid
  • the channels are in communication, wherein each first fluid channel has two first channel openings, each second fluid channel having a second channel opening, wherein the flow field of a previous flow field plate of
  • the present invention still further provides a flow field plate set for a fuel cell, wherein the fuel cell has at least one membrane electrode set including at least two flow field plates, wherein the membrane electrode group of the fuel cell is Separately disposed between two adjacent flow field plates, wherein each flow field plate includes a flow field plate body, a set of first guide walls and a set of second guide walls, wherein the flow field plate body has a cathode side And an anode side, wherein the flow field plate body has at least one fuel passage disposed on the anode side, wherein the first guide wall is spaced apart from the cathode side of the flow field plate, the second The guiding walls respectively extend from the first guiding wall such that adjacent two first guiding walls form a first fluid passage between the two, and the corresponding adjacent two second guiding walls form one at both a second fluid passageway, wherein the first fluid passage is in communication with the second fluid passage, wherein each first fluid passage has two first passage openings, and each second fluid passage has a second passage opening ,
  • FIG. 1A is an assembled view of a flow field plate assembly of a proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
  • FIG. 1B is another assembled view of a flow field plate set of a proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
  • FIG. 2A is a top plan view of a cathode flow field plate of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
  • FIG. 2B is a bottom plan view of a cathode flow field plate of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
  • 3A is a top plan view of an anode flow field plate of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
  • Figure 3B is a bottom plan view of the anode flow field plate of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
  • FIG. 4 illustrates the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the invention described above, wherein the proton exchange membrane fuel cell stack employs the flow field plate set described above.
  • Figure 5A illustrates that the cathode flow field plate and the anode flow field plate of the flow field plate set described above are stacked on each other in the proton exchange membrane fuel cell stack according to a preferred embodiment of the present invention.
  • Figure 5B is a partial cross-sectional view of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
  • Figure 5C is a partial enlarged view of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the invention described above.
  • Figure 6 is a cross-sectional view of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
  • Figure 7A illustrates an alternate implementation of the flow field plate set of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the invention described above.
  • Figure 7B is a partial cross-sectional view of the alternate embodiment of the cathode flow field plate of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
  • Figure 7C is a partial enlarged view of the alternative embodiment of the cathode flow field plate of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
  • Figure 8A illustrates another alternative implementation of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the invention described above.
  • Figure 8B is a cross-sectional view of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
  • Figure 8C is a top plan view of the cathode plate of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
  • Figure 8D is a top plan view of the anode plate body of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
  • Figure 8E is a bottom plan view of the cathode plate of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
  • Figure 8F is a bottom plan view of the anode plate body of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
  • Figure 9A illustrates another alternative implementation of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the invention described above.
  • Figure 9B is a cross-sectional view of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
  • Figure 9C is a top plan view of the support plate of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
  • Figure 9D is a top plan view of the flow field plate of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
  • Figure 9E is a bottom plan view of the support plate of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
  • Figure 9F is a bottom plan view of the flow field plate of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
  • each fuel cell unit of the proton exchange fuel cell stack can be formed as a single fuel cell, including A membrane electrode assembly 10 and a flow field plate assembly 20, wherein the flow field plate assembly 20 includes two electrically conductive bipolar plates to sandwich the membrane electrode assembly 10 therebetween.
  • the membrane electrode assembly 10 includes a polymer electrolyte membrane, and a catalyst coated on both sides of the polymer electrolyte membrane.
  • Two gas diffusion layers are respectively located on both outer sides of the membrane electrode assembly 10 of the membrane electrode assembly, wherein the gas diffusion layer is held between the conductive bipolar plates of the flow field plate group 20 to form a battery cell group.
  • the conductive bipolar plate for sandwiching the flow field plate group 20 between the membrane electrode assembly 10 is an anode flow field plate 21' and a Cathode flow field plate 21.
  • the flow field plate set 20 includes an anode flow field plate 21' and a cathode flow field plate 21, and the membrane electrode assembly 10 is sealed and sandwiched between the anode flow field plate 21' and the cathode flow field plate.
  • the cathode flow field plate 21 has an inner side and an outer side
  • the inner side of the cathode flow field plate 21 forms a planar side 211
  • the outer side of the cathode flow field plate 21 forms a channel side 212.
  • the planar side 211 of the cathode flow field plate 21 is disposed toward the membrane electrode assembly 10, wherein the cathode flow field plate 21 further has a plurality of fluid passages 213 formed in the channel side 212, wherein each fluid passage 213 is a penetrating passage extending from the outer side of the cathode flow field plate 21 to the inner side of the cathode flow field plate 21 to enable fluid to flow along the fluid channel 213 to the membrane electrode assembly 10, thereby promoting electrochemical reaction Electrical energy is generated and generated through the membrane electrode assembly 10.
  • each fluid channel 213 can extend from the planar side 211 of the cathode flow field plate 21 to the channel side 212 of the cathode flow field plate 21 such that fluid can flow along the fluid channel 213 to the membrane electrode set.
  • the fluid passage 213 is a penetrating passage for guiding fluid from the edge of the cathode flow field plate 21 to the inner side of the cathode flow field plate 21, wherein the inner side of the cathode flow field plate 21 faces the inner side Membrane electrode group 10.
  • the fluid is a reactive gas such as air.
  • the fuel cell stack of a proton exchange membrane fuel cell in actual use comprises a plurality of stacked unit fuel assemblies which may be in the hundreds depending on electrical consumption requirements.
  • a typical fuel cell stack includes a collection of repeating battery cells.
  • the cathode flow field plate 21 (or the anode flow field plate 21') may be constructed of a lightweight and strong conductive material.
  • the fluid passage 213 extends to the entire length of the side of the cathode flow field plate 21 and extends into the cathode flow field plate 21 at a predetermined depth.
  • the fluid passage 213 also forms a ridge-like ridge from the uncut cathode flow field plate 21, and these ridge-like projections are uniformly and uniformly distributed.
  • each fluid passage 213 is an elongated passage such that two passage openings are formed at both edges of the cathode flow field plate 21, respectively.
  • the fluid will flow from the passage opening to the fluid passage 213 and through the passage side 212 of the cathode flow field plate 21 to the planar side 211 of the cathode flow field plate 21 to reach the membrane electrode assembly 10.
  • the cathode flow field plate 21 further has a set of cooling channels 217, wherein the cold However, the passage 217 is respectively aligned with the fluid passage 213 to dissipate the heat of the cathode flow field plate 21 when the fluid flows along the fluid passage 213.
  • the cooling passage 217 is a penetrating passage uniformly formed in the cathode flow field plate 21 to be aligned with the fluid passage 213, respectively.
  • the cathode flow field plate 21 includes a cathode plate body 214 and two opposite ends, two first ends 215, wherein the cathode plate body 214 extends in two first portions. Between the ends 215, wherein the cathode plate body 214 includes two lateral edges 2141 and a set of guide walls 216, wherein the guide walls 216 extend spaced apart between the two lateral edges 2141, wherein each two adjacent The guiding wall 216 forms the fluid passage 213 and the cooling passage 217 communicating with the fluid passage 213 therebetween, wherein each cooling passage 217 is disposed along the fluid passage 213 to enable the fluid to flow through the Cooling channel 217.
  • the first end portion 215 of the cathode flow field plate 21 and the two lateral edges 2141 of the cathode plate body 214 form a continuous sealing plane 2110 of the planar side 211 of the cathode flow field plate 21, thereby When the fuel cell stack is stacked, the planar side 211 of the cathode flow field plate 21 can provide a flat support for the membrane electrode assembly 10, thereby enabling the membrane electrode assembly 10 to be pressed against the anode flow field plate 21'. .
  • each of the guide walls 216 includes a high end 2161 and a low end 2162 extending downward from the high end 2161, wherein each two adjacent guide walls 216 are formed at its high end 2161.
  • the fluid passage 213 between and forms the cooling passage 217 between its lower end 2162.
  • the cooling passage 217 communicates with the fluid passage 213 to form a through passage, wherein the through passage allows fluid to flow through the cooling passage 217 and the fluid passage 213.
  • the lower end 2162 is longer than the high end 2161 such that the length of the cooling passage 217 is longer than the length of the fluid passage 213.
  • the structure in which the fluid passage 213 of the cathode flow field plate 21 communicates with the cooling passage 217 to form a completely penetrating passage (or groove) enables the cooling passage 217 to realize the fuel of the present invention.
  • the external reactive fluid is guided to the fluid passage 213.
  • the cooling passage 217 of the cathode flow field plate 21 realizes the dual functions of gas supply and heat dissipation, and the first end portion 215 of the cathode flow field plate 21 and the two lateral edges 2141 of the cathode plate body 214 are
  • the membrane electrode assembly 10 has a larger contact surface, thereby providing the fuel cell stack of the present invention with better heat dissipation and lowering fan speed sensitivity. Accordingly, as the heat dissipation effect increases and the fan speed sensitivity decreases, the overall volume and weight of the fuel cell can be reduced at the same power output relative to the larger fuel cells that need to be constructed in the prior art.
  • the configuration of the cooling passage 217 of the present invention can reduce the thickness of the cathode flow field plate 21.
  • the conventional cathode flow field plate needs to have a thickness of at least 4 mm to maintain the mechanical strength of the cathode flow field plate and ensure heat dissipation efficiency.
  • the cathode flow field plate 21 of the present invention when its fluid passage 213 is set to be 3 mm deep The thickness of the cathode flow field plate 21 can be configured to be less than 4 mm.
  • the cooling passage 217 can be configured as a part of the fluid passage 213 such that the thickness of the cathode flow field plate 21 can be lowered.
  • the cathode flow field plate 21 of the present invention can be thinner than a conventional stencil when achieving the same heat dissipating area; because the cooling passage 217 of the present invention can pass the cathode flow when the fluid passes through the fluid passage 213
  • the entire cross section of the field plate 21 serves as heat dissipation. Therefore, the cathode flow field plate 21 of the present invention can provide more heat dissipation regions for heat dissipation at the same thickness as conventional panels.
  • the anode flow field plate 21' of the flow field plate group 20 has an inner side and an outer side, wherein the inner and outer sides of the anode flow field plate 21' are both planar sides.
  • the inner side of the anode flow field plate 21' forms a channel side 212' and the outer side forms a planar side 211', wherein the channel side 212' of the anode flow field plate 21' forms at least one fuel passage 213', wherein
  • the fuel passage 213' faces the membrane electrode assembly 10 such that a fuel, such as hydrogen fuel, can be supplied to the membrane electrode assembly 10 through the fuel passage 213'.
  • the fuel passage 213' is recessed in the passage side 212' of the anode flow field plate 21'.
  • the anode flow field plate 21' includes an anode plate body 214' and two opposite ends, two second ends 215', wherein the anode plate body 214' extends at the two second ends 215
  • the anode plate body 214' and the second end portion 215' of the anode flow field plate 21' form a continuous sealing plane 2120' formed on the channel side 212' of the anode flow field plate 21'.
  • the planar side 211 of the cathode flow field plate 21 of the flow field plate group 20 and the channel side 212' of the anode flow field plate 21' can be the film respectively.
  • the electrode assembly 10 provides a flat support, and the planar side 211 of the cathode flow field plate 21 and the channel side 212' of the anode flow field plate 21' are sealingly pressed against the membrane electrode assembly 10.
  • the flow field plate set 20 further includes a gasket 22, wherein the gasket 22 is disposed on the membrane electrode assembly 10 and the anode flow field plate 21', wherein A gasket 22 is disposed on the channel side 212' of the anode flow field plate 21'.
  • each adjacent two fuel cells are assembled to each other, and the planar side 211' of the anode flow field plate 21' of the previous fuel cell Coupling with the channel side 212 of the cathode flow field plate 21 of the next fuel cell, wherein the planar side 211' of the anode flow field plate 21' of the previous fuel cell and the cathode flow field of the next fuel cell
  • the channel side 212 of the plate 21 defines two fluid flow channels 2150 therebetween, wherein the fluid flow channels 2150 are in communication with the fuel passages 213', respectively, to enable fuel to pass from the fuel flow path 2150 through the fuel.
  • Channel 213' flows to another fluid flow channel 2150.
  • each fluid flow path 2150 has a first opening 21501' and a second opening 21502', wherein the first opening 21501' and the second opening 21502' are both formed at the anode.
  • the first opening 21501' of the flow channel 2150 and the second opening 21502' prevent fuel from leaking from the gap between the membrane electrode assembly 10 and the channel side 212' of the anode flow field plate 21'.
  • each fuel passage 213' is in communication with two fluid flow passages 2150, respectively, to allow fuel to flow from one fluid flow passage 2150 through the fuel passage 213' to the other fluid flow passage 2150.
  • the first opening 21501' and the second opening 21502' of the fluid flow path 2150 are respectively two penetrating holes formed in the two second end portions 215' of the anode flow field plate 21'. And are set to align with each other.
  • each fuel passage 213 is disposed between the second end portion 215' of the anode flow field plate 21' and has a serpentine structure to extend the flow distance of the fuel, wherein each fuel passage 213' The two ends are respectively connected to the second opening 21502', as shown in FIG. 3B of the drawing.
  • fuel is directed through the fuel passage 213' between the two second openings 21502' of the second end 215' of the anode flow field plate 21'.
  • the fuel passage 213' can also be provided with other suitable shapes.
  • each fluid flow path 2150 is formed on the channel side 212 of the cathode flow field plate 21, wherein each first end portion 215 of the cathode flow field plate 21 further has a set A sealing groove 21502 surrounding the fluid flow path 2150.
  • the sealing groove 21502 is a groove formed in the channel side 212 of the cathode flow field plate 21 to surround the fluid channel 2150.
  • the flow field plate set 20 further includes two sealing rings 23, wherein the sealing ring 23 is respectively disposed in the sealing groove 21502 to prevent fuel from the planar side 211' of the anode flow field plate 21' and the cathode flow field plate. The gap between the channel sides 212 of 21 leaks.
  • each fluid flow path 2150 further has a third opening 21501 formed in the first end portion 215 of the cathode flow field plate 21, wherein the third opening 2501 passes through the cathode Flow field plate 21. It is noted that when a group of fuel cells are stacked on each other to form a fuel cell stack, the third opening 21501 of the first end portion 215 of the cathode flow field plate 21 and the corresponding anode flow field plate The second opening 21502' of the second end 215' of 21' forms a fuel flow passage 200 such that hydrogen fuel can be supplied through the fuel flow passage 200 of the fuel cell stack.
  • the fluid flow channel 2150 is formed on the planar side 211' of the anode flow field plate 21' and the two sealing grooves 21502 are respectively disposed around the fluid flow channel 2150, wherein the flow field plate group 20 further includes Two seal rings 23, wherein the seal rings 23 are respectively disposed in the seal groove 21502 to prevent fuel from between the plane side 211' of the anode flow field plate 21' and the channel side 212 of the cathode flow field plate 21 The gap leaks.
  • the gasket 22 of the battery cell of the fuel cell stack has a hollow structure to achieve a sealing portion on the channel side of the anode flow field plate 21'.
  • the gasket 22 is a hollow structure to allow a fluid, such as a gas, to pass therethrough.
  • the gasket 22 is further sized and shaped to match the channel side 212' of the anode flow field plate 21'. Seal of the gasket 22 as shown in FIG. 3B Portions are respectively disposed at the second end portion 215' of the anode flow field plate 21' and the anode plate body 214' to form a closed environment for hydrogen flow. It will be appreciated that the fuel passage 213' is not covered by the gasket 22.
  • Figure 3B of the accompanying drawings also shows a fuel cell stack design in accordance with a preferred embodiment of the present invention, i.e., regardless of the type of sealing employed, such as an adhesive pad, the adhesive pad is in a compressed state.
  • the gasket 22 of the present invention can be a loop gasket or an adhesive gasket.
  • the gasket 22 is preferably a gasket structure made of a flexible material disposed on the channel side 212' of the anode flow field plate 21' to prevent hydrogen leakage when the stack is in operation. Therefore, the flow field plate assembly 20 requires only one gasket 22 to achieve a seal between the planar side 211 of the cathode flow field plate 21 and the channel side 212' of the anode flow field plate 21'.
  • the planar side 211 of the cathode flow field plate 21 is mounted to the membrane electrode assembly 10.
  • the proton exchange membrane fuel cell is configured to be open to the atmosphere, and therefore an oxidant such as air (or oxygen) is blown into the fluid passage 213 through the cathode flow field plate 21.
  • the configuration of the cooling passage 217 enhances air cooling efficiency because heat is dissipated and separated through the cooling passage 217.
  • the cooling passage 217 enhances the heat dissipation effect and enables the cathode flow field plate 21 to be thinner than the conventional type. A thinner and lighter fuel cell stack can make it more portable than the prior art.
  • the cooling passage 217 is molded from the cathode flow field plate 21 to reduce the sensitivity of the film moisture content to the fan speed.
  • the cooling passage 217 is formed with respect to each fluid passage 213.
  • the cooling passage 217 and the fluid passage 213 will maintain the water content of the membrane electrode assembly 10 because the heat dissipation gas flow through the cooling passage 217 is not in direct contact with the membrane electrode assembly 10. Therefore, when the fan speed increases or slows down, only part of the airflow directly affects the water content of the membrane electrode assembly 10, but all airflows have a cooling effect. In other words, the battery voltage of the fuel cell becomes less sensitive to the fan speed.
  • the cathode flow field plate 21 provided by the present invention can likewise provide heat and water management for the fuel cell. Accordingly, the membrane electrode assembly 10 requires a high water content to maintain a low internal resistance. When the gas is blown into and through the fluid passage 213, it is cooled only by the cooling passage 217, and the cathode flow field plate 21 does not accelerate the evaporation of water to prevent the water content of the membrane electrode assembly 10 from being lowered.
  • the bright flow field plate set 20 can make the difference between the fuel cell stacks smaller.
  • the fuel cells using the flow field plate set 20 of the present invention have uniformity between them. Therefore, the fuel cell stack provided by the present invention can more easily achieve the uniformity of the battery voltage by being able to adopt a higher hydrogen pressure.
  • FIG. 7A through 7C illustrate an alternate implementation of the cathode flow field plate 21 of the flow field plate set 20 of the fuel cell stack in accordance with a preferred embodiment of the present invention, wherein the flow field plate set 20A A cathode flow field plate 21A and an anode flow field plate 21' are included, wherein the cathode flow field plate 21A has a planar side 211A and a channel side 212A, and includes a cathode plate body 214A and two opposite ends, two First end portions 215A, wherein the cathode plate body 214A extends between the first end portions 215A, wherein the cathode plate body 214A includes two lateral edges 2141A and a set of guiding walls 216A, wherein the guiding walls 216A are respectively Separably disposed between the lateral edges 2141A, wherein each two adjacent 216A form a fluid passage 213A therebetween, and each guide wall 216A forms a cooling passage 217A, wherein the cooling passage
  • each flow field plate 21C includes a cathode plate body 211C, an anode plate body 212C and a set of guide walls 213C, wherein the cathode plate body 211C forms a set of first fluid grooves 2110C spaced apart from each other, wherein The guiding wall 213C is disposed between the cathode plate body 211C and the anode plate body 212C so as to be spaced apart such that each adjacent two guiding walls 213C form a second fluid groove 2130C therebetween.
  • the first fluid groove 2110C of the cathode plate body 211C is disposed to be in parallel with and in communication with the second fluid groove 2130C, respectively, such that each of the first fluid grooves 2110C forms a continuous fluid passage with the corresponding second fluid groove 2130C.
  • the fluid passage 214C has a first passage opening 2141C, a second passage opening 2142C, and a third passage opening 2143C, wherein the third passage opening 2143C of the fluid passage 214C is disposed toward the membrane electrode assembly 10, thereby
  • the fluid passage 214C is allowed to allow a reactive material fluid such as air, oxygen, or the like to flow between the first passage opening 2141C of the fluid passage 214C and the second passage opening 2142C, and is supplied to the third passage opening 2143C through the third passage opening 2143C
  • the length of the first fluid groove 2110C is greater than the length of the second fluid groove 2130C, and the width of the first fluid groove 2110C is smaller than the width of the second fluid groove 2130C.
  • each flow field plate 21C has a first channel side 215C and a second channel side 216C, wherein the first channel side 215C of the cathode plate body 211C is formed at the cathode.
  • An outer side of the plate body 211C, the second channel side 216C of the anode plate body 212C is formed on an outer side of the anode plate body 212C, wherein the flow field plate 21C has at least one portion disposed on the flow field plate 21C
  • Two-channel side 216C fuel passage 217C, and the second channel side 216C of the flow field plate 21C are disposed toward the membrane electrode assembly 10 such that a fuel, such as hydrogen, can be supplied to the membrane electrode assembly 10 through the fuel passage 217C.
  • the first fluid groove 2110C of the cathode plate body 211C is formed on the outer side of the cathode plate body 211C
  • the fuel passage 217C of the anode plate body 212C is formed on the outer side of the anode plate body 212C.
  • the flow field plate group 20C of the fuel cell includes at least two flow field plates 21C, wherein each of the membrane electrode groups 10 is disposed adjacent to two
  • the second channel side 216C of the previous flow field plate 21C in the flow field plate is between the first channel side 215C of the subsequent flow field plate 21C.
  • the second channel side 216C of the previous one of the adjacent flow field plates 21C, the first channel side 215C of the latter flow field plate 21C, and the membrane electrode assembly 10 form a battery cell .
  • the guide wall 213C of each flow field plate 21C of the flow field plate group 20C is disposed on one inner side of the anode plate body 212C, and from the anode plate body 212C. This inner side extends.
  • the guiding wall 213C of the flow field plate 21C is integrally formed with the anode plate body 212C. More preferably, the cathode plate body 211C of the flow field plate 21C of the flow field plate group 20C is detachably disposed at the guide wall 213C.
  • the cathode plate body 211C of the flow field plate 21C of the flow field plate group 20C has a receiving groove 218C formed on one inner side of the cathode plate body 211C, wherein the receiving portion 218C is accommodated therein.
  • the shape and size of the groove 218C are set according to the guide wall 213C of the flow field plate 21C to accommodate the guide wall 213C of the flow field plate 21C therein, and the second fluid formed by the guide wall 213C
  • the grooves 2130C are respectively in line with and in communication with the first fluid groove 2110C of the cathode plate body 211C, thereby forming the fluid passage 214C.
  • the depth of the receiving groove 218C is the same as the height of the guiding wall 213C of the flow field plate 21C, so that the guiding wall 213C of the flow field plate 21C can be accommodated in the cathode plate body 211C.
  • the receiving groove 218C is the same as the height of the guiding wall 213C of the flow field plate 21C, so that the guiding wall 213C of the flow field plate 21C can be accommodated in the cathode plate body 211C.
  • the cathode plate body 211C of the flow field plate 21C of the flow field plate group 20C includes two opposite end portions, and the two first end portions 2111C and the two extend respectively.
  • a first lateral edge 2112C between the first end portion 2111C and a first forming portion 2113C extending longitudinally between the first lateral edge 2112C, wherein the first forming portion 2113C is formed to extend in the first lateral direction a first fluid groove 2110C between the edges 2112C, wherein the first end portion 2111C of the cathode plate body 211C and the first lateral edge 2112C form a continuous sealing plane 2150C on the first channel side 215C of the flow field plate 21C
  • the continuous sealing plane 2150C is disposed around the first forming portion 2113C of the cathode plate body 211C;
  • the anode plate body 212C of the flow field plate 21C includes two opposite ends, two second ends 2121C, Two second
  • the second forming portion 2123C such that the first channel side 215C and the second channel side 216C of the flow field plate 21C can provide a flat level for the membrane electrode assembly 10 when the fuel cell stack is stacked
  • the first channel side 215C and the second channel side 216C of the flow field plate 21C are supported and sealed against the membrane electrode assembly 10.
  • first fluid tank 2110C of the cathode plate body 211C of the flow field plate 21C communicates with the second fluid tank 2130C to form a fully penetrating fluid passage 214C (or groove).
  • the structure allows the second fluid tank 2130C to function to direct the external reactive fluid to the first fluid tank 2110C while achieving the heat dissipation function of the fuel cell stack of the present invention.
  • the second fluid groove 2130C of the flow field plate 21C realizes the dual functions of gas supply and heat dissipation, and the first end portion 2111C and the lateral edge 2112C of the cathode plate body 211C and the membrane electrode assembly 10 have one
  • the larger contact surface allows the fuel cell stack of the present invention to have better heat dissipation and reduce fan speed sensitivity. Accordingly, as the heat dissipation effect increases and the fan speed sensitivity decreases, the overall volume and weight of the fuel cell can be reduced at the same power output relative to the larger fuel cells that need to be constructed in the prior art.
  • the configuration of the fluid passage 214C of the present invention can reduce the thickness of the cathode plate body 211C (or the cathode flow field plate).
  • the conventional cathode flow field plate needs to have a thickness of at least 4 mm to maintain the mechanical strength of the cathode flow field plate and ensure heat dissipation efficiency.
  • the thickness of the cathode plate body 211C can be configured to be less than 4 mm.
  • the second fluid tank 2130C can be configured as part of the fluid passage 214C such that the thickness of the cathode plate body 211C can be lowered.
  • the cathode plate body 211C of the present invention can be thinner than the conventional cathode flow field plate when the same heat dissipation area is realized; because the second fluid groove 2130C of the present invention can be used when the fluid passes through the fluid passage 214C The entire cross section of the cathode plate body 211C is used as heat dissipation. Therefore, the cathode plate body 211C of the present invention can provide more heat dissipation regions for heat dissipation at the same thickness as conventional panels.
  • each first end portion 2111C of the cathode plate body 211C of the flow field plate 21C of the flow field plate group 20C has a first communication opening 21110C
  • the anode plate body Each of the second ends 2121C of the 212C has a second communication opening 21210C, wherein the first communication opening 21110C of the first end portion 2111C of the cathode plate body 211C and the corresponding anode plate body 212C are respectively
  • the second communication opening 21210C of the two end portions 2121C communicates with each other and forms a fuel flow path 200C, wherein both ends of each of the fuel passages 217C of the flow field plate 21C are respectively communicated with the fuel flow path 200C, thereby causing hydrogen fuel Passing the fuel cell stack
  • the fuel flow path 200C of the flow field plate 21C of the flow field plate group 20C is supplied.
  • the seal between the adjacent two flow field plates 21C of the flow field plate group 20C can be realized by a gasket 22C, wherein the gasket 22C is a hollow structure. And the sealing portion of the gasket 22C is disposed on the outer circumference of the anode plate body 212C of the previous flow field plate 21C.
  • the gasket 22C is a hollow structure to allow a fluid, such as a gas, to pass therethrough.
  • the gasket 22C is further provided in a size and shape that matches the outer side of the anode plate body 212C. As shown in FIG. 8A to FIG.
  • the gaskets 22C are respectively disposed on the outer side of the anode plate body 212C of the previous flow field plate 21C of two adjacent flow field plates 21C, wherein the gasket 22C is a hollow. Structure, and a sealing portion of the gasket 22C is disposed between the anode plate body 212C of the previous flow field plate 21C and the cathode plate body 211C of the subsequent flow field plate 21C and the periphery of the membrane electrode group 10 is disposed Between the sealing portion of the gasket 22C and the anode plate body 212C of the previous flow field plate 21C, so that the anode plate body 212C of the previous flow field plate 21C, the cathode plate body of the latter flow field plate 21C 211C and the membrane electrode assembly 10 form a sealed space for fuel flow.
  • both ends of the gasket 22C are respectively disposed at the end of the anode plate body 212C of the previous flow field plate 21C and the end portion of the cathode flow field plate 211C of the corresponding subsequent flow field plate 21C.
  • the second opening 2110C is such that when the fuel cell is assembled and the gasket 22C is squeezed between the two flow field plates 21C, the anode plate body 212C and the latter flow field plate of the previous flow field plate 21C
  • the cathode plates 211C of 21C are sealedly stacked on each other to prevent leakage of fuel from the gap between the anode plate body 211C of the previous flow field plate 21C and the cathode plate body 211C of the latter flow field plate 21C.
  • the fuel passage 217C is not covered by the gasket 22C.
  • the gasket 22C is further disposed at both ends of the cathode plate body 211C and the fuel passage 217C surrounding the anode plate body 212C to form a sealed space for hydrogen flow.
  • the fuel passage 217C is not covered by the gasket 22C.
  • the first end portion 2111C of the cathode plate body 211C of the flow field plate 21C of the flow field plate group 20C is separately and sealingly disposed on the anode plate body 212C.
  • the second end portion 2121C prevents the hydrogen fuel from passing through the first end portion 2111C of the cathode plate body 211C of the flow field plate 21C of the flow field plate group 20C and the corresponding second end portion 2121C of the anode plate body 212C.
  • the first end portion 2111C of the cathode plate body 211C of the flow field plate 21C of the flow field plate group 20C and the second end portion 2121C of the corresponding anode plate body 212C are sealingly coupled to each other.
  • the first end portion 2111C of the cathode plate body 211C and the second end portion 2121C of the corresponding anode plate body 212C are formed to form a gap between the two communicating with the fuel flow path 200C.
  • the seal between the second end portion 2121C of the plate body 212C may pass through the first communication opening 21110C (or around the corresponding anode plate body 212C) disposed around the first end portion 2111C of the cathode plate body 211C.
  • the seal ring or gasket 23C of the second communication opening 21210C) of the second end portion 2121C is realized.
  • the sealing between the first end portion 2111C of the cathode plate body 211C and the second end portion 1211C of the corresponding anode plate body 212C passes through the first end of the cathode plate body 211C.
  • the portion 2111C and the corresponding second end portion 2121C of the anode plate body 212C are brought into close contact with each other to be realized.
  • the sealing between the first end portion 2111C of the cathode plate body 211C and the second end portion 2121C of the corresponding anode plate body 212C is performed by using a glue or an adhesive to the cathode plate body 211C.
  • the first end portion 2111C and the second end portion 1211C of the corresponding anode plate body 212C are adhered together to be realized.
  • FIGS 9A through 9F illustrate another alternative implementation of the flow field plate set 20D of the fuel cell stack in accordance with a preferred embodiment of the present invention, wherein the flow field plate set 20D includes at least two flow fields The plate 21D, wherein each flow field plate 21D includes a flow field plate 211D, a set of first guide walls 212D, and a set of second guide walls 213D, wherein the flow field plate 211D has a cathode side 2111D and an anode side 2112D, wherein the flow field plate 211D has at least one fuel passage 215D disposed on the anode side 2112D, wherein the first guide wall 212D is spaced apart from the cathode side 2111D of the flow field plate 211D,
  • the second guiding walls 213D respectively extend from the first guiding wall 212D such that each adjacent two guiding walls 212D form a first fluid passage 216D between the two, and corresponding two adjacent The second guide wall 213D forms a second fluid passage 2
  • the first fluid passage 216D allows a fluid such as air or oxygen to flow from one first passage opening 2161D to the other first passage opening 2161D. Therefore, the first fluid passage 216D provides a reaction in the phase of the membrane electrode assembly 10. At the same time as the active material, it also has a cooling effect.
  • the length of the first fluid passage 216D is greater than the length of the second fluid passage 217D, and the width of the first fluid passage 216D is smaller than the width of the second fluid passage 217D.
  • the flow field plate group 20D includes at least two flow field plates 21D, wherein the fuel cell Each membrane electrode group 10 of the fuel cell unit of the stack is disposed between two adjacent flow field plates 21D of the flow field plate group 20D, wherein the previous flow field plate 21D of the adjacent two flow field plates 21D
  • the second fluid passage 217D and the fuel passage 215D of the latter flow field plate 21D are respectively disposed toward the membrane electrode assembly 10 such that a reactive substance such as air, and a fuel such as hydrogen can pass through the second fluid, respectively.
  • a channel 217D and the fuel channel 215D are supplied to the membrane electrode assembly 10.
  • each flow field plate 21D of the flow field plate group 20D further includes a support plate 214D, wherein the support plate 214D is disposed at the first guide wall 212D, wherein the support The plate 214D forms a receiving groove 2140D, and when the supporting plate 214D is disposed at the first guiding wall 212D, the second guiding wall 213D of the flow field plate 21D is accommodated in the receiving groove 2140D of the supporting plate 214D.
  • the height of the second guiding wall 213D of the flow field plate 21D is not greater than the depth of the receiving groove 2140D of the supporting plate 214D, so that the second guiding wall 213D of the flow field plate 21D is accommodated therein.
  • the receiving groove 214D is received in the receiving groove 2140D.
  • the length of the first guiding wall 212D of the flow field plate 21D of the flow field plate group 20D is greater than the length of the second guiding wall 213D, so that the supporting plate 214D can be disposed at the first guiding wall 212D.
  • the second guiding wall 213D extends from the middle portion of the first guiding wall 212D such that both first lateral edges 2142D of the supporting plate 214D can be disposed at the top end of the first guiding wall 212D.
  • the support plate 214D is detachably disposed on the first guide wall 212D.
  • the alternately implemented support plate 214D of the flow field plate set 20D of the fuel cell stack in accordance with a preferred embodiment of the present invention functions as an assembly support in the fuel cell stack of the present invention.
  • the support plate 214D of the flow field plate 21D of the flow field plate set 20D may not involve providing the membrane electrode assembly 10 with a reactive substance or fuel. Therefore, the support plate 214D of the flow field plate 21D of the flow field plate group 20D can be made of a non-conductive rigid material. That is, the support plate 214D of the flow field plate 21D of the flow field plate group 20D can be made of a material having high strength and low weight to reduce the weight-to-power ratio of the fuel cell stack.
  • the support plate 214D of the flow field plate 21D of the flow field plate group 20D has an outer side and an inner side, wherein the outer side of the support plate 214D is disposed toward the film electrode.
  • the continuous sealing plane 21120D of the anode side 2112D is disposed around the fuel passage 215D such that when the fuel cell stack is stacked, the outer side of the support plate 214D of the flow field plate 21D and the anode side 2112D can respectively
  • the membrane electrode assembly 10 provides a flat support, and the outer side of the support plate 214D and the anode side 2112D of the flow field plate 211D can be sealingly pressed against the membrane electrode assembly 10, respectively.
  • the support plate 214D of the flow field plate 21D of the flow field plate group 20D includes two opposite ends, and the two first end portions 2141D and the two extend respectively. a first lateral edge 2142D between the first end portions 2141D, wherein the first end portion 2141D of the support plate 214D and the first lateral edge 2142D form the receiving groove 2140D and the continuous sealing plane 210D;
  • the flow field plate The flow field plate 211D of 21D includes two opposite ends, two second ends 2113D, two second lateral edges 2114D extending between the second ends 2113D and a longitudinal extension a forming portion 2115D between the second lateral edges 2114D, wherein the forming portion 2115D forms a fuel passage 215D extending between the second end portions 2113D, wherein the second end portion 2113D of the flow field plate body 211D and the first portion
  • the second lateral edge 2114D forms the continuous sealing plane 21120D on the anode side
  • first fluid passage 216D of the flow field plate 21D communicates with the second fluid passage 217D to form a completely penetrating passage (or groove).
  • the first fluid passage 216D can be made. While the heat dissipation function of the fuel cell stack of the present invention is achieved, the external reactive fluid is guided to the second fluid passage 217D.
  • the first fluid channel 216D of the flow field plate 21D achieves the dual functions of air supply and heat dissipation, and the first end portion 2141D and the first lateral edge 2142D of the support plate 214D and the membrane electrode assembly 10 have A larger contact surface, such that when the support plate 214D is made of a good thermally conductive material, the fuel cell stack of the present invention has better heat dissipation and reduced fan speed sensitivity. Accordingly, as the heat dissipation effect increases and the fan speed sensitivity decreases, the overall volume and weight of the fuel cell can be reduced at the same power output relative to the larger fuel cells that need to be constructed in the prior art.
  • the support plate 214D of the flow field plate 21D of the flow field plate group 20D includes two first end portions 2141D, and the flow field plate body of the flow field plate 21D.
  • 211D includes two opposite ends, two second ends 2113D, wherein each first end 2141D of the support plate 214D of the flow field plate 21D of the flow field plate group 20D has a first communication opening 21410D,
  • Each of the second end portions 2113D of the flow field plate 211D has a second communication opening 21130D, wherein the first communication opening 21410D of the first end portion 2141D of the support plate 214D and the corresponding flow field plate respectively
  • the second communication opening 21130D of the second end portion 2113D of the body 211D communicates with and forms a fuel flow path 200D, wherein both ends of each fuel passage 215D of the flow field plate 21D are respectively connected to the fuel flow path 200D.
  • the seal between the adjacent two flow field plates 21D of the flow field plate group 20D can be realized by a gasket 22D which is a hollow structure. And the sealing portion of the gasket 22D is disposed on one circumference of the anode side 2112D of the flow field plate 211D of the previous flow field plate 21D.
  • the gasket 22D is a hollow structure to allow a fluid, such as a gas, to pass therethrough.
  • the gasket 22D is further provided in a size and shape that matches the anode side 2112D of the flow field plate 211D. As shown in FIGS.
  • the gasket 22D is a hollow structure, and the sealing portion of the gasket 22D is disposed in the flow field plate of the previous flow field plate 21D of the two adjacent flow field plates 21D.
  • the anode side 2112D of the body 211D and the support plate 214D of the latter flow field plate 21D wherein a circumference of the membrane electrode assembly 10 is disposed at the sealing portion of the gasket 22D and the previous flow field plate 21D
  • the anode side 2112D of the flow field plate 211D is such that the flow field plate 211D of the previous flow field plate 21D, the support plate 214D of the latter flow field plate 21D, and the membrane electrode assembly 10 form a sealed space.
  • both ends of the gasket 22D are respectively disposed at the end of the flow field plate 211D of the previous flow field plate 21D and the end portion of the support plate 214D of the corresponding subsequent flow field plate 21D. And wherein the gasket 22D is disposed to surround the two of the second communication opening 21130D of the flow field plate 211D of the previous flow field plate 21D and the two support plates 214D of the subsequent flow field plate 21D, respectively.
  • a communication opening 21410D such that when the fuel cell is assembled and the gasket 22D is squeezed between two adjacent flow field plates 21D, the flow field plate 211D and the latter of the previous flow field plate 21D
  • the support plates 214D of the flow field plate 21D are sealedly stacked on each other to prevent fuel from being between the flow field plate 211D of the previous flow field plate 21D and the flow field plate 211D of the latter flow field plate 21D.
  • the gap leaks.
  • the fuel passage 215D is not covered by the gasket 22D.
  • the gasket 22D is further disposed at both ends of the support plate 214D and the fuel passage 215D surrounding the flow field plate 211D to form a sealed space for hydrogen flow. In other words, the fuel passage 215D is not covered by the gasket 22D.
  • the first end portion 2141D of the support plate 214D of the flow field plate 21D of the flow field plate group 20D is separately and sealingly disposed on the flow field plate body 211D.
  • a second end portion 2113D for preventing hydrogen fuel from passing through the first end portion 2141D of the support plate 214D of the flow field plate 21D of the flow field plate group 20D and the corresponding second end portion 2113D of the flow field plate body 211D The gap between the leaks. Therefore, the first end portion 2141D of the support plate 214D of the flow field plate 21D of the flow field plate group 20D and the corresponding second end portion 2113D of the flow field plate body 211D are sealingly coupled to each other.
  • the first end portion 2141D of the support plate 214D and the corresponding second end portion 2113D of the flow field plate body 211D are formed to form a gap between the two communicating with the fuel flow path 200D.
  • the seal between the second end portion 2113D of the field plate body 211D may pass through the first communication opening 21410D disposed around the first end portion 2141D of the support plate 214D (or around the corresponding flow field plate body 211D)
  • the seal ring or seal ring 23D of the second communication opening 21130D) of the second end portion 2113D is realized.
  • the seal between the first end 2141D of the support plate 214D of the flow field plate 21D and the second end portion 2113D of the corresponding flow field plate 211D passes the support plate 214D.
  • the first end portion 2141D and the corresponding second end portion 2113D of the flow field plate body 211D are closely attached to each other.
  • the seal between the first end 2141D of the support plate 214D and the corresponding second end portion 2113D of the flow field plate 211D is achieved by using glue or adhesive to the support plate 214D.
  • the first end portion 2141D and the corresponding second end portion 2113D of the flow field plate body 211D are adhered together to be realized.
  • anode flow field plate anode plate body or flow field plate body
  • cathode flow field plate cathode plate body or flow field plate body
  • the material is typically a conductive metal.
  • the metal is strong, lightweight and electrically conductive, but the material is not limited to metal.
  • Conductive composite materials containing graphite, carbon black, carbon fibers, and/or nanocarbons, or even materials such as conductive graphite, carbon black, carbon fibers, and/or nanocarbon, which are reinforced, can be used in the structure of the present invention.

Abstract

A cathode flow field plate (21) for use in a fuel cell. The fuel cell has a membrane electrode assembly (10), and the cathode flow field plate (21) is arranged to seal the membrane electrode assembly (10). The cathode flow field plate (21) has a set of fluid channels (213) and a set of cooling channels (217), and the cooling channels (217) are respectively aligned and in communication with the fluid channels (213).

Description

PEM燃料电池堆及其流场板组PEM fuel cell stack and its flow field plate set 技术领域Technical field
本发明涉及燃料电池技术领域,尤其涉及用于质子交换膜(PEM)燃料电池的聚合物薄膜电池堆。The present invention relates to the field of fuel cell technology, and more particularly to a polymer thin film battery stack for a proton exchange membrane (PEM) fuel cell.
背景技术Background technique
燃料电池是一种能量源,其可通过反应活性物质,如氧或其它氧化剂参与的化学反应将来自燃料的化学能转化为电能。氢是此类电池中最常见的燃料。其中,最具代表性的此类燃料电池技术的实例就是质子交换薄膜(PEM)燃料电池。此类燃料电池包括膜电极组(MEA),该膜电极组包括夹在分别作为阴阳级的两层催化剂涂层纸间的聚合物电解质膜;该膜电极组(MEA)再夹在一对流场板之间,其分别关系到燃料和氧化剂。该燃料电池的工作原理包括以下步骤:将氢燃料通入燃料电池一侧的阳极流场板中,再将氧化剂通入燃料电池另一侧的阴极流场板中;将铂催化剂(或其它催化剂)置于阳极侧使得氢分离为正电荷氢质子和负电荷氢电子;聚合物电解质膜仅可使正电荷氢质子穿过后进入阴极,而负电荷氢电子则需要通过外设的通道进入阴极,此时电流即产生;在阴极侧,电子和正电荷质子与氧结合生成水,作为该电池排出唯一产物。此外,因为氧气是被吹入阴极流场板,故可使该燃料电池冷却。阴极流场板可采用暴露于空气中作为一种“开放阴极结构”。A fuel cell is an energy source that converts chemical energy from a fuel into electrical energy through a chemical reaction involving a reactive species, such as oxygen or other oxidant. Hydrogen is the most common fuel in such batteries. Among them, the most representative example of such a fuel cell technology is a proton exchange membrane (PEM) fuel cell. Such a fuel cell includes a membrane electrode assembly (MEA) including a polymer electrolyte membrane sandwiched between two layers of catalyst coated papers respectively as yin and yang grades; the membrane electrode assembly (MEA) is sandwiched between a pair of streams Between field plates, they are related to fuel and oxidant, respectively. The working principle of the fuel cell comprises the steps of: passing hydrogen fuel into an anode flow field plate on one side of the fuel cell, and then passing the oxidant into a cathode flow field plate on the other side of the fuel cell; and a platinum catalyst (or other catalyst) On the anode side, hydrogen is separated into positively charged hydrogen protons and negatively charged hydrogen electrons; the polymer electrolyte membrane can only pass positively charged hydrogen protons into the cathode, while negatively charged hydrogen electrons need to enter the cathode through the channels of the peripherals. At this point, current is generated; on the cathode side, electrons and positively charged protons combine with oxygen to form water, which is the only product discharged from the battery. In addition, since oxygen is blown into the cathode flow field plate, the fuel cell can be cooled. The cathode flow field plate can be exposed to air as an "open cathode structure."
传统的阴极流场板设计采用锯状或方波状结构,空气可通过鼓风机或风扇吹入其中。相较水冷却型电池堆,空气冷却型电池堆具有更易平衡设计和更易控制策略,其可被立即启动。The traditional cathode flow field plate design uses a saw-like or square wave structure, and air can be blown into it by a blower or a fan. Compared to water-cooled cell stacks, air-cooled cell stacks have a more balanced design and easier control strategy that can be activated immediately.
采用聚合物电解质薄膜的空气冷却型质子交换薄膜燃料电池的一个主要技术难点是热量和水处理管理。其中聚合物电解质薄膜需要具备高含水量以保持薄膜的内在低电阻。当气流通过流场板通道时,可冷却电池堆,但同样加速了水分的蒸发导致薄膜中水含量降低。因此,风扇转速需要根据流量、环境温度和相对湿度极为小心的控制(控制策略)以达到平衡。不适当的风扇转速将导致电池堆的输出功率下降。One of the main technical difficulties of air-cooled proton exchange membrane fuel cells using polymer electrolyte membranes is heat and water treatment management. Among them, the polymer electrolyte membrane needs to have a high water content to maintain the inherent low resistance of the film. When the gas stream passes through the flow field plate channel, the cell stack can be cooled, but the evaporation of moisture is also accelerated to cause a decrease in water content in the film. Therefore, the fan speed needs to be carefully controlled (control strategy) based on flow, ambient temperature and relative humidity to achieve equilibrium. Improper fan speed will cause the output power of the stack to drop.
采用聚合物电解质薄膜的空气冷却型质子交换薄膜燃料电池的另一个限制是氢渗漏。在传统设计中,锯状阴极流场板面向膜电极组,其包括聚合物电解质薄膜以及两侧的催化剂层。因此,仅有锯齿压在垫圈之上,该区域的其他部分未收到锯齿的压力和难以被密封,以致成为潜在氢渗漏区域。另外,该设计一般限定了氢工作压力小于0.5bar.g。然而,较高的氢压力可以促进动力学、电池均一性、负载变化响应和降低氢饥饿(严重损害燃料电 池的耐久度)发生概率,但高于设计压力值却可能会导致泄漏或垫圈爆裂。Another limitation of air-cooled proton exchange membrane fuel cells employing polymer electrolyte membranes is hydrogen leakage. In a conventional design, the saw-like cathode flow field plate faces the membrane electrode assembly, which includes a polymer electrolyte membrane and catalyst layers on both sides. Therefore, only the serrations are pressed against the gasket, and other portions of the region are not subjected to the pressure of the serrations and are difficult to be sealed, so as to become potential hydrogen leakage regions. Additionally, the design generally defines a hydrogen working pressure of less than 0.5 bar.g. However, higher hydrogen pressures can promote kinetics, battery uniformity, load change response, and reduced hydrogen starvation (serious damage to fuel power) The durability of the pool), but higher than the design pressure value may cause leakage or gasket burst.
发明内容Summary of the invention
本发明的主要目的在于其提供一种燃料电池,其中该燃料电池结合有用于质子交换膜燃料电池的流场板组,以防止氢渗漏。A primary object of the present invention is to provide a fuel cell in which a flow field plate set for a proton exchange membrane fuel cell is incorporated to prevent hydrogen leakage.
本发明的另一目的是提供一种流场板组,其中该流场板组允许更高燃料电池工作压力和提高冷却效率。此性能提升了作为高能量密度能量来源的燃料电池的功率重量比和续航能力。Another object of the present invention is to provide a flow field plate set that allows for higher fuel cell operating pressures and improved cooling efficiency. This performance increases the power-to-weight ratio and endurance of a fuel cell as a source of high energy density energy.
本发明的另一目的是提供一种流场板组,其中该流场板组的阴极流场板的内侧和阳极流场板的内侧形成两个相面对面的连续平面,从而使得该流场板组的阴极流场板的内侧和阳极流场板的内侧之间仅需设置一个密封膜即可实现该阴极流场板的内侧和该阳极流场板的内侧之间的密封。进一步地,该流场板组的单个密封膜实现该阴极流场板的内侧和该阳极流场板的内侧之间的密封,使得该流场板组的装配难度的降低。Another object of the present invention is to provide a flow field plate set in which the inner side of the cathode flow field plate of the flow field plate group and the inner side of the anode flow field plate form two continuous faces facing each other, thereby making the flow field plate A seal between the inner side of the cathode flow field plate and the inner side of the anode flow field plate is achieved by providing only one sealing film between the inner side of the cathode flow field plate and the inner side of the anode flow field plate. Further, the single sealing film of the flow field plate group realizes the sealing between the inner side of the cathode flow field plate and the inner side of the anode flow field plate, so that the assembly difficulty of the flow field plate group is reduced.
本发明的另一目的是提供一种用于质子交换薄膜燃料电池的流场板组,以实现该质子交换薄膜燃料电池能够在压力大于0.5bar.g条件下工作而不发生氢泄漏和因此而操作更为安全。Another object of the present invention is to provide a flow field plate set for a proton exchange membrane fuel cell to enable the proton exchange membrane fuel cell to operate at a pressure greater than 0.5 bar.g without hydrogen leakage and thus The operation is safer.
本发明的另一目的是提供一种用于质子交换薄膜燃料电池的流场板组,以实现该质子交换薄膜燃料电池能够在压力大于0.5bar.g条件下工作,从而使得该燃料电池相比于传统型燃料电池,其动力学、电池一致性、负载变化响应被提升和氢饥饿产生概率被降低。Another object of the present invention is to provide a flow field plate set for a proton exchange membrane fuel cell to enable the proton exchange membrane fuel cell to operate at a pressure greater than 0.5 bar.g, thereby allowing the fuel cell to be compared In conventional fuel cells, the kinetics, battery uniformity, load change response are increased and the probability of hydrogen starvation is reduced.
本发明的另一目的是提供一种用于质子交换薄膜燃料电池的流场板组,以提升空气冷却效率,从而允许使用更薄的能够降低总重功率比的流场板。Another object of the present invention is to provide a flow field plate set for a proton exchange membrane fuel cell to enhance air cooling efficiency, thereby allowing the use of a thinner flow field plate capable of reducing the total weight to power ratio.
本发明的另一目的是提供一种用于质子交换薄膜燃料电池的流场板组,以降低质子交换膜的水含量对风扇转速的敏感性。Another object of the present invention is to provide a flow field plate set for a proton exchange membrane fuel cell to reduce the sensitivity of the water content of the proton exchange membrane to the fan speed.
本发明的另一目的是提供一种用于质子交换薄膜燃料电池的流场板组,其中该流场板组的新设计的流场板更容易实现密封和防止氢泄漏。Another object of the present invention is to provide a flow field plate set for a proton exchange membrane fuel cell wherein the newly designed flow field plate of the flow field plate set is easier to seal and prevent hydrogen leakage.
本发明的另一目的是提供一种用于质子交换薄膜燃料电池的流场板组,其中该新设计的流场板可适用于装配在大多数传统质子交换薄膜燃料电池。Another object of the present invention is to provide a flow field plate set for a proton exchange membrane fuel cell, wherein the newly designed flow field plate can be adapted for assembly in most conventional proton exchange membrane fuel cells.
本发明的另一目的是提供一种用于质子交换薄膜燃料电池的流场板组,其中该新设计的流场板易于使用、结构简单和制造成本低廉。Another object of the present invention is to provide a flow field plate set for a proton exchange membrane fuel cell wherein the newly designed flow field plate is easy to use, simple in construction, and inexpensive to manufacture.
本发明的其它目的和特点通过下述的详细说明得以充分体现并可通过所附权利要求中特地指出的手段和装置的组合得以实现。 Other objects and features of the present invention will be realized and at the
依本发明,前述目的和其他目的和优势通过一种气冷质子交换燃料电池堆被实现。In accordance with the present invention, the foregoing and other objects and advantages are realized by an air-cooled proton exchange fuel cell stack.
依本发明,前述目的和其他目的和优势通过一种燃料电池被实现,其中该燃料电池包括一膜电极组和一流场板组。In accordance with the present invention, the foregoing and other objects and advantages are realized by a fuel cell including a membrane electrode assembly and a first-rate field plate assembly.
该流场板组包括一个阴极流场板和一个阳极流场板,其中该膜电极组被密封于该阴极流场板和该阳极流场板之间,其中该阴极流场板具有一平面侧、一相反的通道侧和一组形成在该通道侧的流体通道,其中该平面侧位于该阴极流场板的一朝向膜电极组的外侧,其中该流体通道被设置用于使流体能够沿该流体通道流向该膜电极组,从而促进电化学反应穿过该膜电极发生和产生电能,其中该阳极流场板具有一个平面侧、一个相反的通道侧和至少一个燃料通道,其中该阳极流场板的该平面侧位于该阳极流场板的一个内侧,该阳极流场板的该通道侧位于该阳极流场板的一个外侧和密封该膜电极组,其中该阳极流场板的每个该燃料通道形成在该阳极流场板的该通道侧,其中该燃料通道被设置用于使燃料能够通过该燃料通道被提供给该膜电极组。The flow field plate set includes a cathode flow field plate and an anode flow field plate, wherein the membrane electrode assembly is sealed between the cathode flow field plate and the anode flow field plate, wherein the cathode flow field plate has a planar side An opposite channel side and a plurality of fluid channels formed on the channel side, wherein the planar side is located outside of the cathode flow field plate toward the outside of the membrane electrode set, wherein the fluid channel is configured to enable fluid along the Fluid channels are directed to the set of membrane electrodes to facilitate electrochemical reaction to generate and generate electrical energy through the membrane electrode, wherein the anode flow field plate has a planar side, an opposite channel side, and at least one fuel passage, wherein the anode flow field The planar side of the plate is located on an inner side of the anode flow field plate, the channel side of the anode flow field plate is located on an outer side of the anode flow field plate and seals the membrane electrode set, wherein each of the anode flow field plates A fuel passage is formed on the passage side of the anode flow field plate, wherein the fuel passage is configured to enable fuel to be supplied to the membrane electrode assembly through the fuel passage.
相应地,本发明进一步提供一种用于燃料电池的阴极流场板,其中该燃料电池具有一个膜电极组,其包括一个阴极流场板,其中该阴极流场板被布置以密封该膜电极组,其中该阴极流场板具有一组流体通道和一组冷却通道,其中该冷却通道分别与该流体通道相对其和相连通。Accordingly, the present invention further provides a cathode flow field plate for a fuel cell, wherein the fuel cell has a membrane electrode set including a cathode flow field plate, wherein the cathode flow field plate is arranged to seal the membrane electrode The set wherein the cathode flow field plate has a plurality of fluid passages and a set of cooling passages, wherein the cooling passages are respectively in communication with the fluid passages.
相应地,本发明进一步提供一种用于燃料电池的阳极流场板,其中该燃料电池具有一个膜电极组,其包括一个阳极流场板,其中该阳极流场板具有一个平面侧和一个通道侧,其中该平面侧位于该阳极流场板的一个内侧,其中该通道侧位于该阳极流场板的一个外侧,其中该阳极流场板的该通道侧被设置适用于密封该膜电极组,其中该阳极流场板进一步包括至少一个燃料通道,其中该燃料通道形成于朝向该膜电极组的该通道侧,从而使燃料能够通过该燃料通道被提供给该膜电极组。Accordingly, the present invention further provides an anode flow field plate for a fuel cell, wherein the fuel cell has a membrane electrode set including an anode flow field plate, wherein the anode flow field plate has a planar side and a channel a side, wherein the planar side is located on an inner side of the anode flow field plate, wherein the channel side is located on an outer side of the anode flow field plate, wherein the channel side of the anode flow field plate is configured to seal the membrane electrode set, Wherein the anode flow field plate further includes at least one fuel passage, wherein the fuel passage is formed toward the passage side of the membrane electrode assembly such that fuel can be supplied to the membrane electrode assembly through the fuel passage.
本发明还进一步提供一种用于燃料电池的流场板组,其中该燃料电池具有至少一个膜电极组,其包括至少两个流场板,其中该燃料电池的该膜电极组被分别设置在相邻两个流场板之间,其中每个流场板包括一个阴极板体、一个阳极板体和一组引导墙,其中该阴极板体形成一组相互隔开的第一流体槽,其中该引导墙被相隔开地设置在该阴极板体和该阳极板体之间,从而使得每相邻两个引导墙形成一个位于两者之间的第二流体槽,其中该阴极板体的该第一流体槽被设置分别与该第二流体槽相连通,从而使得每个第一流体槽与相应的第二流体槽形成至少一个连续的流体通道,其中该流体通道具有一个第一通道开口、一个第二通道开口和一个第三通道开口,其中该流场板的该阳极板体具有至少一个被设置 在该阳极板体的一个外侧的燃料通道,其中每相邻两个流场板的前一个流场板的该阳极板体的该外侧被设置朝向该燃料电池的被设置在相邻两个流场板之间的该膜电极组,从而使燃料能够通过该燃料通道被提供给该膜电极组,后一个流场板的该阴极板体的该流体通道的该第三通道开口被设置朝向该膜电极组,从而使得该流体通道允许流体流动在该流体通道的该第一通道开口和该第二通道开口之间,并通过该第三通道开口被提供给该燃料电池的该膜电极组The present invention still further provides a flow field plate set for a fuel cell, wherein the fuel cell has at least one membrane electrode set including at least two flow field plates, wherein the membrane electrode groups of the fuel cell are respectively disposed at Between two adjacent flow field plates, wherein each flow field plate comprises a cathode plate body, an anode plate body and a set of guide walls, wherein the cathode plate body forms a set of first fluid grooves spaced apart from each other, wherein The guiding wall is spaced apart between the cathode plate body and the anode plate body such that each adjacent two guiding walls form a second fluid groove between the two, wherein the cathode plate body The first fluid grooves are disposed to communicate with the second fluid grooves, respectively, such that each of the first fluid grooves and the corresponding second fluid grooves form at least one continuous fluid passage, wherein the fluid passage has a first passage opening a second passage opening and a third passage opening, wherein the anode plate body of the flow field plate has at least one set a fuel passage on an outer side of the anode plate body, wherein the outer side of the anode plate body of the previous flow field plate of each adjacent two flow field plates is disposed toward the fuel cell and disposed adjacent to the two streams The membrane electrode assembly between the field plates such that fuel can be supplied to the membrane electrode assembly through the fuel passage, the third passage opening of the fluid passage of the cathode plate body of the latter flow field plate being disposed toward the membrane electrode assembly a membrane electrode assembly such that the fluid passage allows fluid to flow between the first passage opening and the second passage opening of the fluid passage and is supplied to the membrane electrode assembly of the fuel cell through the third passage opening
本发明还进一步提供一种燃料电池,其包括至少一个膜电极组和一个流场板组,其中该流场板组包括至少两个流场板,其中该膜电极组分别被设置在相邻两个流场板之间,其中每个流场板包括一个阴极板体、一个阳极板体和一组引导墙,其中该阴极板体形成一组相互隔开的第一流体槽,其中该引导墙被相隔开地设置在该阴极板体和该阳极板体之间,从而使得每相邻两个引导墙形成一个位于两者之间的第二流体槽,其中该阴极板体的该第一流体槽被设置分别与该第二流体槽相连通,从而使得每个第一流体槽与相应的第二流体槽形成至少一个连续的流体通道,其中该流体通道具有一个第一通道开口、一个第二通道开口和一个第三通道开口,其中该流场板的该阳极板体具有至少一个被设置在该阳极板体的一个外侧的燃料通道,其中相邻两个流场板的前一个流场板的该阳极板体的该外侧被设置朝向被设置在相邻两个流场板之间的该膜电极组,从而使燃料能够通过该燃料通道被提供给该膜电极组,后一个流场板的该阴极板体的该流体通道的该第三通道开口被设置朝向该膜电极组,从而使得该流体通道允许流体流动在该流体通道的该第一通道开口和该第二通道开口之间,并通过该第三通道开口被提供给该膜电极组。The present invention still further provides a fuel cell comprising at least one membrane electrode assembly and one flow field plate group, wherein the flow field plate group comprises at least two flow field plates, wherein the membrane electrode groups are respectively disposed adjacent to the two Between the flow field plates, wherein each flow field plate comprises a cathode plate body, an anode plate body and a set of guide walls, wherein the cathode plate body forms a set of spaced apart first fluid grooves, wherein the guide wall Separably disposed between the cathode plate body and the anode plate body such that each adjacent two guide walls form a second fluid groove therebetween, wherein the first portion of the cathode plate body The fluid slots are disposed in communication with the second fluid channels, respectively, such that each of the first fluid channels and the respective second fluid grooves form at least one continuous fluid passage, wherein the fluid passage has a first passage opening, a first a two-channel opening and a third passage opening, wherein the anode plate body of the flow field plate has at least one fuel passage disposed on an outer side of the anode plate body, wherein a previous one of the adjacent two flow field plates The outer side of the anode plate body of the flow field plate is disposed toward the membrane electrode group disposed between adjacent two flow field plates, thereby enabling fuel to be supplied to the membrane electrode group through the fuel passage, the latter The third passage opening of the fluid passage of the cathode plate body of the flow field plate is disposed toward the membrane electrode assembly such that the fluid passage allows fluid to flow in the first passage opening and the second passage opening of the fluid passage Between and through the third passage opening is provided to the membrane electrode assembly.
相应地,本发明还进一步提供一种一种用于燃料电池的流场板组,其中该燃料电池具有至少一个膜电极组,其包括至少两个流场板,其中该燃料电池的该膜电极组被分别设置在相邻两个流场板之间,其中每个流场板包括一个阴极板体、一个阳极板体和一组引导墙,其中该阴极板体形成一组相互隔开的第一流体槽,其中该引导墙被相隔开地设置在该阴极板体和该阳极板体之间,从而使得每相邻两个引导墙形成一个位于两者之间的第二流体槽,其中该阴极板体的该第一流体槽被设置分别与该第二流体槽相连通,从而使得每个第一流体槽与相应的第二流体槽形成至少一个连续的流体通道,其中该流体通道具有一个第一通道开口、一个第二通道开口和一个第三通道开口,其中该流场板的该阳极板体具有至少一个被设置在该阳极板体的一个外侧的燃料通道,其中每相邻两个流场板的前一个流场板的该阳极板体的该外侧被设置朝向该燃料电池的被设置在相邻两个流场板之间的该膜电极组,从而使燃料能够通过该燃料通道被提供给该膜电极组,后一个流场板的该阴极 板体的该流体通道的该第三通道开口被设置朝向该膜电极组,从而使得该流体通道允许流体流动在该流体通道的该第一通道开口和该第二通道开口之间,并通过该第三通道开口被提供给该燃料电池的该膜电极组。Accordingly, the present invention still further provides a flow field plate set for a fuel cell, wherein the fuel cell has at least one membrane electrode set including at least two flow field plates, wherein the membrane electrode of the fuel cell The groups are respectively disposed between two adjacent flow field plates, wherein each flow field plate includes a cathode plate body, an anode plate body and a set of guide walls, wherein the cathode plate body forms a set of mutually separated first a fluid groove, wherein the guide wall is spaced apart between the cathode plate body and the anode plate body such that each adjacent two guide walls form a second fluid groove between the two, wherein The first fluid grooves of the cathode plate body are disposed to communicate with the second fluid grooves, respectively, such that each of the first fluid grooves and the corresponding second fluid grooves form at least one continuous fluid passage, wherein the fluid passage has a first passage opening, a second passage opening and a third passage opening, wherein the anode plate body of the flow field plate has at least one fuel passage disposed on an outer side of the anode plate body, The outer side of the anode plate body of the preceding flow field plate of each adjacent two flow field plates is disposed toward the membrane electrode group of the fuel cell disposed between adjacent two flow field plates, thereby Fuel can be supplied to the membrane electrode set through the fuel passage, the cathode of the latter flow field plate The third passage opening of the fluid passage of the plate body is disposed toward the membrane electrode assembly such that the fluid passage allows fluid to flow between the first passage opening and the second passage opening of the fluid passage, and passes through the A third passage opening is provided to the membrane electrode set of the fuel cell.
本发明还进一步提供一种燃料电池,其包括至少一个膜电极组和至少两个流场板,其中该膜电极组被分别设置在相邻两个流场板之间,其中每个流场板包括一个流场板体、一组第一引导墙和一组第二引导墙,其中该流场板体具有一个阴极侧和一个阳极侧,其中该流场板体具有至少一个被设置在该阳极侧的燃料通道,其中该第一引导墙被相隔开地设置在该流场板体的该阴极侧,该第二引导墙分别自该第一引导墙延伸,从而使得相邻两个第一引导墙形成一个位于两者之间的第一流体通道,和相应的相邻两个第二引导墙形成一个位于两者之间的第二流体通道,其中该第一流体通道与该第二流体通道相连通,其中每个第一流体通道具有两个第一通道开口,每个第二流体通道具有一个第二通道开口,其中相邻两个流场板的前一个流场板的该流场板体的该阳极侧被设置朝向被设置在相邻两个流场板之间的该膜电极组,从而使燃料能够通过该燃料通道被提供给该膜电极组,和后一个流场板的该流场板体的该第二流体通道的该第二通道开口被设置朝向该燃料电池的该膜电极组,从而使得该第一流体通道允许流体流动在该流体通道的该第一通道开口之间,并通过该第二流体通道的该第二通道开口被提供给该燃料电池的该膜电极组。The present invention still further provides a fuel cell comprising at least one membrane electrode set and at least two flow field plates, wherein the membrane electrode sets are respectively disposed between adjacent two flow field plates, wherein each flow field plate The invention comprises a flow field plate body, a set of first guiding walls and a set of second guiding walls, wherein the flow field plate body has a cathode side and an anode side, wherein the flow field plate body has at least one disposed at the anode a side fuel passage, wherein the first guide wall is spaced apart from the cathode side of the flow field plate, the second guide wall respectively extending from the first guide wall, so that two adjacent first The guiding wall forms a first fluid passage between the two, and the corresponding adjacent two second guiding walls form a second fluid passage therebetween, wherein the first fluid passage and the second fluid The channels are in communication, wherein each first fluid channel has two first channel openings, each second fluid channel having a second channel opening, wherein the flow field of a previous flow field plate of two adjacent flow field plates The anode of the plate Provided toward the membrane electrode assembly disposed between adjacent two flow field plates such that fuel can be supplied to the membrane electrode assembly through the fuel passage, and the flow field plate of the latter flow field plate The second passage opening of the second fluid passage is disposed toward the membrane electrode assembly of the fuel cell such that the first fluid passage allows fluid to flow between the first passage opening of the fluid passage and passes through the first The second passage opening of the two fluid passage is provided to the membrane electrode assembly of the fuel cell.
相应地,本发明还进一步提供一种用于燃料电池的流场板组,其中该燃料电池具有至少一个膜电极组,其包括至少两个流场板,其中该燃料电池的该膜电极组被分别设置在相邻两个流场板之间,其中每个流场板包括一个流场板体、一组第一引导墙和一组第二引导墙,其中该流场板体具有一个阴极侧和一个阳极侧,其中该流场板体具有至少一个被设置在该阳极侧的燃料通道,其中该第一引导墙被相隔开地设置在该流场板体的该阴极侧,该第二引导墙分别自该第一引导墙延伸,从而使得相邻两个第一引导墙形成一个位于两者之间的第一流体通道,和相应的相邻两个第二引导墙形成一个位于两者之间的第二流体通道,其中该第一流体通道与该第二流体通道相连通,其中每个第一流体通道具有两个第一通道开口,每个第二流体通道具有一个第二通道开口,其中相邻两个流场板的前一个流场板的该流场板体的该阳极侧被设置朝向被设置在相邻两个流场板之间的该膜电极组,从而使燃料能够通过该燃料通道被提供给该膜电极组,和后一个流场板的该流场板体的该第二流体通道的该第二通道开口被设置朝向该燃料电池的该膜电极组,从而使得该第一流体通道允许流体流动在该流体通道的该第一通道开口之间,并通过该第二流体通道的该第二通道开口被提供给该燃料电池的该膜电极组。 Accordingly, the present invention still further provides a flow field plate set for a fuel cell, wherein the fuel cell has at least one membrane electrode set including at least two flow field plates, wherein the membrane electrode group of the fuel cell is Separately disposed between two adjacent flow field plates, wherein each flow field plate includes a flow field plate body, a set of first guide walls and a set of second guide walls, wherein the flow field plate body has a cathode side And an anode side, wherein the flow field plate body has at least one fuel passage disposed on the anode side, wherein the first guide wall is spaced apart from the cathode side of the flow field plate, the second The guiding walls respectively extend from the first guiding wall such that adjacent two first guiding walls form a first fluid passage between the two, and the corresponding adjacent two second guiding walls form one at both a second fluid passageway, wherein the first fluid passage is in communication with the second fluid passage, wherein each first fluid passage has two first passage openings, and each second fluid passage has a second passage opening , The anode side of the flow field plate of the previous flow field plate of the adjacent two flow field plates is disposed toward the membrane electrode group disposed between the adjacent two flow field plates, thereby enabling fuel to pass The fuel passage is provided to the membrane electrode assembly, and the second passage opening of the second fluid passage of the flow field plate of the latter flow field plate is disposed toward the membrane electrode assembly of the fuel cell such that the The first fluid passage allows fluid to flow between the first passage opening of the fluid passage and is provided to the membrane electrode assembly of the fuel cell through the second passage opening of the second fluid passage.
通过对随后的描述和附图的理解,本发明进一步的目的和优势将得以充分体现。Further objects and advantages of the present invention will be fully realized from the understanding of the appended claims.
本发明的这些和其它目的、特点和优势,通过下述的详细说明,附图和权利要求得以充分体现。These and other objects, features and advantages of the present invention will become apparent from
附图说明DRAWINGS
图1A是根据本发明优选实施例的质子交换膜燃料电池堆的流场板组的装配图。1A is an assembled view of a flow field plate assembly of a proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
图1B是根据上述本发明优选实施例的质子交换膜燃料电池堆的流场板组的另一装配图。1B is another assembled view of a flow field plate set of a proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
图2A是根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的阴极流场板的俯视图。2A is a top plan view of a cathode flow field plate of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
图2B是根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的阴极流场板的仰视图。2B is a bottom plan view of a cathode flow field plate of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
图3A是根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的阳极流场板的俯视图。3A is a top plan view of an anode flow field plate of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
图3B是根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的阳极流场板的仰视图。Figure 3B is a bottom plan view of the anode flow field plate of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
图4阐明了根据上述本发明优选实施例的该质子交换膜燃料电池堆,其中该质子交换膜燃料电池堆采用了上述流场板组。4 illustrates the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the invention described above, wherein the proton exchange membrane fuel cell stack employs the flow field plate set described above.
图5A阐明了上述流场板组的阴极流场板和阳极流场板在根据本发明优选实施例的该质子交换膜燃料电池堆中被相互堆叠在一起。Figure 5A illustrates that the cathode flow field plate and the anode flow field plate of the flow field plate set described above are stacked on each other in the proton exchange membrane fuel cell stack according to a preferred embodiment of the present invention.
图5B是根据上述本发明优选实施例的该质子交换膜燃料电池堆的部分剖视图。Figure 5B is a partial cross-sectional view of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
图5C是根据上述本发明优选实施例的该质子交换膜燃料电池堆的部分放大图。Figure 5C is a partial enlarged view of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the invention described above.
图6是根据上述本发明优选实施例的该质子交换膜燃料电池堆的剖视图。Figure 6 is a cross-sectional view of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
图7A阐明了根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的一种可选实施。Figure 7A illustrates an alternate implementation of the flow field plate set of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the invention described above.
图7B是根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的该阴极流场板的该可选实施的部分剖视图。Figure 7B is a partial cross-sectional view of the alternate embodiment of the cathode flow field plate of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
图7C是根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的该阴极流场板的该可选实施的部分放大图。Figure 7C is a partial enlarged view of the alternative embodiment of the cathode flow field plate of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
图8A阐明了根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的另一种可选实施。 Figure 8A illustrates another alternative implementation of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the invention described above.
图8B是根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的该可选实施的该流场板的剖视图。Figure 8B is a cross-sectional view of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
图8C是根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的该可选实施的该流场板的该阴极板体的俯视图。Figure 8C is a top plan view of the cathode plate of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
图8D是根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的该可选实施的该流场板的该阳极板体的俯视图。Figure 8D is a top plan view of the anode plate body of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
图8E是根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的该可选实施的该流场板的该阴极板体的仰视图。Figure 8E is a bottom plan view of the cathode plate of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
图8F是根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的该可选实施的该流场板的该阳极板体的仰视图。Figure 8F is a bottom plan view of the anode plate body of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
图9A阐明了根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的另一种可选实施。Figure 9A illustrates another alternative implementation of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the invention described above.
图9B是根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的该可选实施的该流场板的剖视图。Figure 9B is a cross-sectional view of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention described above.
图9C是根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的该可选实施的该流场板的该支撑板的俯视图。Figure 9C is a top plan view of the support plate of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
图9D是根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的该可选实施的该流场板的该流场板体的俯视图。Figure 9D is a top plan view of the flow field plate of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
图9E是根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的该可选实施的该流场板的该支撑板的仰视图。Figure 9E is a bottom plan view of the support plate of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
图9F是根据上述本发明优选实施例的该质子交换膜燃料电池堆的该流场板组的该可选实施的该流场板的该流场板体的仰视图。Figure 9F is a bottom plan view of the flow field plate of the flow field plate of the alternate embodiment of the flow field plate stack of the proton exchange membrane fuel cell stack in accordance with a preferred embodiment of the present invention.
具体实施方式detailed description
下述描述被揭露以使本领域技术人员可制造和使用本发明。下述描述中提供的较佳实施例仅作为对本领域技术人员显而易见的示例和修改,其并不构成对本发明范围的限制。下述描述中所定义的一般原理可不背离本发明精神和发明范围地应用于其它实施例、可选替代、修改、等同实施和应用。The following description is disclosed to enable any person skilled in the art to make and use the invention. The preferred embodiments provided in the following description are merely exemplary and modifications that are obvious to those skilled in the art, and are not intended to limit the scope of the invention. The general principles defined in the following description may be applied to other embodiments, alternatives, modifications, equivalents and applications without departing from the spirit and scope of the invention.
参考附图之图1A至图6,依本发明较佳实施例的质子交换燃料电池堆被阐明。该质子交换燃料电池堆包括一个或多个相互堆叠在一起的燃料电池单元。依本发明较佳实施例,该质子交换燃料电池堆的每个燃料电池单元可形成作为一个单独的燃料电池,其包括 一个膜电极组10和一个流场板组20,其中该流场板组20包括两个电导通的双极板以将该膜电极组10夹在两者之间。Referring to Figures 1A through 6 of the drawings, a proton exchange fuel cell stack in accordance with a preferred embodiment of the present invention is illustrated. The proton exchange fuel cell stack includes one or more fuel cell units stacked on each other. According to a preferred embodiment of the invention, each fuel cell unit of the proton exchange fuel cell stack can be formed as a single fuel cell, including A membrane electrode assembly 10 and a flow field plate assembly 20, wherein the flow field plate assembly 20 includes two electrically conductive bipolar plates to sandwich the membrane electrode assembly 10 therebetween.
该膜电极组10包括一个聚合物电解质膜,以及涂布于该聚合物电解质膜两侧的催化剂。两气体扩散层分别位于该膜电极组件该膜电极组10的两外侧面,其中该气体扩散层被保持在该流场板组20的该导电双极板之间,以形成一电池单元组。The membrane electrode assembly 10 includes a polymer electrolyte membrane, and a catalyst coated on both sides of the polymer electrolyte membrane. Two gas diffusion layers are respectively located on both outer sides of the membrane electrode assembly 10 of the membrane electrode assembly, wherein the gas diffusion layer is held between the conductive bipolar plates of the flow field plate group 20 to form a battery cell group.
如附图之图1A至图6所示,该用于夹住该膜电极组10于两者之间的该流场板组20的该导电双极板为一个阳极流场板21'和一个阴极流场板21。换句话说,该流场板组20包括一个阳极流场板21′和一个阴极流场板21,且该膜电极组10被密封和夹在该阳极流场板21′和该阴极流场板21之间,其中该阴极流场板21具有一个内侧和一个外侧,其中该阴极流场板21的该内侧形成一个平面侧211,和该阴极流场板21的该外侧形成一个通道侧212,其中该阴极流场板21的该平面侧211被设置朝向该膜电极组10,其中该阴极流场板21进一步具有一组形成在该通道侧212的流体通道213,其中每个流体通道213均为自该阴极流场板21的该外侧延伸至该阴极流场板21的该内侧的穿透型通道,以使流体能够沿该流体通道213流向该膜电极组10,从而促进电化学反应穿过该膜电极组10发生和产生电能。换句话说,每个流体通道213可自该阴极流场板21的该平面侧211延伸至该阴极流场板21的该通道侧212,从而使得流体能够沿该流体通道213流向该膜电极组10。尤其是,该流体通道213为穿透型通道,以用于引导流体自该阴极流场板21的边缘流向该阴极流场板21的该内侧,其中该阴极流场板21的该内侧朝向该膜电极组10。相应地,该流体为反应气体,如空气。As shown in FIGS. 1A to 6 of the accompanying drawings, the conductive bipolar plate for sandwiching the flow field plate group 20 between the membrane electrode assembly 10 is an anode flow field plate 21' and a Cathode flow field plate 21. In other words, the flow field plate set 20 includes an anode flow field plate 21' and a cathode flow field plate 21, and the membrane electrode assembly 10 is sealed and sandwiched between the anode flow field plate 21' and the cathode flow field plate. Between 21, wherein the cathode flow field plate 21 has an inner side and an outer side, wherein the inner side of the cathode flow field plate 21 forms a planar side 211, and the outer side of the cathode flow field plate 21 forms a channel side 212. Wherein the planar side 211 of the cathode flow field plate 21 is disposed toward the membrane electrode assembly 10, wherein the cathode flow field plate 21 further has a plurality of fluid passages 213 formed in the channel side 212, wherein each fluid passage 213 is a penetrating passage extending from the outer side of the cathode flow field plate 21 to the inner side of the cathode flow field plate 21 to enable fluid to flow along the fluid channel 213 to the membrane electrode assembly 10, thereby promoting electrochemical reaction Electrical energy is generated and generated through the membrane electrode assembly 10. In other words, each fluid channel 213 can extend from the planar side 211 of the cathode flow field plate 21 to the channel side 212 of the cathode flow field plate 21 such that fluid can flow along the fluid channel 213 to the membrane electrode set. 10. In particular, the fluid passage 213 is a penetrating passage for guiding fluid from the edge of the cathode flow field plate 21 to the inner side of the cathode flow field plate 21, wherein the inner side of the cathode flow field plate 21 faces the inner side Membrane electrode group 10. Accordingly, the fluid is a reactive gas such as air.
可以理解的是,实际使用中的质子交换膜燃料电池的该燃料电池堆包括多个堆叠单元燃料集合,根据电消耗要求,其数量可能数以百计。因此,一个典型燃料电池堆包括一系列的重复电池单元集合。该阴极流场板21(或阳极流场板21')可由轻便且坚固的导电材料构成。该流体通道213延伸至该阴极流场板21的整个侧边长度且按预设的深度延伸至该阴极流场板21内。该流体通道213同样自未经切割的该阴极流场板21形成山脊状隆起部,且这些山脊状突起部为分隔地、均一地的分布。It will be appreciated that the fuel cell stack of a proton exchange membrane fuel cell in actual use comprises a plurality of stacked unit fuel assemblies which may be in the hundreds depending on electrical consumption requirements. Thus, a typical fuel cell stack includes a collection of repeating battery cells. The cathode flow field plate 21 (or the anode flow field plate 21') may be constructed of a lightweight and strong conductive material. The fluid passage 213 extends to the entire length of the side of the cathode flow field plate 21 and extends into the cathode flow field plate 21 at a predetermined depth. The fluid passage 213 also forms a ridge-like ridge from the uncut cathode flow field plate 21, and these ridge-like projections are uniformly and uniformly distributed.
如附图之图2A和图2B,每个流体通道213是一个加长通道,从而使得两个通道开口被分别形成在该阴极流场板21的两个边缘。因此,该流体将自该通道开口流向该流体通道213和穿过该阴极流场板21的该通道侧212流向该阴极流场板21的该平面侧211,以到达该膜电极组10。2A and 2B, each fluid passage 213 is an elongated passage such that two passage openings are formed at both edges of the cathode flow field plate 21, respectively. Thus, the fluid will flow from the passage opening to the fluid passage 213 and through the passage side 212 of the cathode flow field plate 21 to the planar side 211 of the cathode flow field plate 21 to reach the membrane electrode assembly 10.
如附图之图2B和图6,该阴极流场板21进一步具有一组冷却通道217,其中该冷 却通道217分别与该流体通道213相对齐,以在当该流体沿该流体通道213流动时,使该阴极流场板21的热被散热。优选地,该冷却通道217为均匀形成在该阴极流场板21的穿透型通道,以分别与该流体通道213相对齐。2B and FIG. 6, the cathode flow field plate 21 further has a set of cooling channels 217, wherein the cold However, the passage 217 is respectively aligned with the fluid passage 213 to dissipate the heat of the cathode flow field plate 21 when the fluid flows along the fluid passage 213. Preferably, the cooling passage 217 is a penetrating passage uniformly formed in the cathode flow field plate 21 to be aligned with the fluid passage 213, respectively.
如附图之图2A至图3B,该阴极流场板21包括一个阴极板体214和两个相反的端部,两个第一端部215,其中该阴极板体214延伸在两个第一端部215之间,其中该阴极板体214包括两个横向边缘2141和一组引导墙216,其中该引导墙216相隔开地延伸在两个横向边缘2141之间,其中每两个相邻的引导墙216形成该流体通道213和与该流体通道213相连通的冷却通道217在两者之间,其中每个冷却通道217被设置沿该流体通道213,以使该流体能够流动穿过该冷却通道217。优选地,该阴极流场板21的该第一端部215和该阴极板体214的两个横向边缘2141形成该阴极流场板21的该平面侧211的一个连续密封平面2110,从而使得当该燃料电池堆被堆叠时,该阴极流场板21的该平面侧211能够为该膜电极组10提供一个平的支撑,从而使该膜电极组10能够抵压在该阳极流场板21′。2A to 3B, the cathode flow field plate 21 includes a cathode plate body 214 and two opposite ends, two first ends 215, wherein the cathode plate body 214 extends in two first portions. Between the ends 215, wherein the cathode plate body 214 includes two lateral edges 2141 and a set of guide walls 216, wherein the guide walls 216 extend spaced apart between the two lateral edges 2141, wherein each two adjacent The guiding wall 216 forms the fluid passage 213 and the cooling passage 217 communicating with the fluid passage 213 therebetween, wherein each cooling passage 217 is disposed along the fluid passage 213 to enable the fluid to flow through the Cooling channel 217. Preferably, the first end portion 215 of the cathode flow field plate 21 and the two lateral edges 2141 of the cathode plate body 214 form a continuous sealing plane 2110 of the planar side 211 of the cathode flow field plate 21, thereby When the fuel cell stack is stacked, the planar side 211 of the cathode flow field plate 21 can provide a flat support for the membrane electrode assembly 10, thereby enabling the membrane electrode assembly 10 to be pressed against the anode flow field plate 21'. .
如附图之图2A和图6所示,每个引导墙216包括一个高端2161和一个自该高端2161向下延伸的低端2162,其中每两个相邻的引导墙216形成位于其高端2161之间的该流体通道213和形成位于其低端2162之间的该冷却通道217。因此,该冷却通道217与该流体通道213相连通以形成一个穿透型通道,其中该穿透型通道允许流体流过该冷却通道217和该流体通道213。可选地,该低端2162长于该高端2161,从而使得该冷却通道217的长度长于该流体通道213的长度。As shown in Figures 2A and 6 of the drawings, each of the guide walls 216 includes a high end 2161 and a low end 2162 extending downward from the high end 2161, wherein each two adjacent guide walls 216 are formed at its high end 2161. The fluid passage 213 between and forms the cooling passage 217 between its lower end 2162. Accordingly, the cooling passage 217 communicates with the fluid passage 213 to form a through passage, wherein the through passage allows fluid to flow through the cooling passage 217 and the fluid passage 213. Optionally, the lower end 2162 is longer than the high end 2161 such that the length of the cooling passage 217 is longer than the length of the fluid passage 213.
可以理解的是,位于该阴极流场板21的该流体通道213与该冷却通道217相连通以形成一个完全穿透型通道(或槽)的这种结构可使该冷却通道217实现本发明燃料电池堆的散热功能的同时,起到将外部反应活性流体引导至该流体通道213的作用。进一步地,该阴极流场板21的该冷却通道217实现供气和散热的双重功能,且该阴极流场板21的该第一端部215、该阴极板体214的两个横向边缘2141与该膜电极组10具有一个更大的接触面,从而使本发明燃料电池堆具有更好的散热效果和降低风扇转速敏感度。相应地,随着散热效应的提升和风扇转速敏感度的降低,在相同功率输出下,相对于现有技术需要构建的更大型的燃料电池,该燃料电池的整体体积和重量均能够被降低。此外,本发明该冷却通道217的构造可降低该阴极流场板21的厚度。如果传统型阴极流场板的流体通道设计为3mm深度,则传统型阴极流场板需至少4mm厚度,以保持阴极流场板的机械强度和确保散热效率。而如果是本发明阴极流场板21,则当其流体通道213被设置为3mm深 度时,该阴极流场板21的厚度则可配置为小于4mm。换言之,该冷却通道217可作为该流体通道213的一部分的配置,使得该阴极流场板21的厚度可被降低。也就是说,在实现相同散热面积时,本发明的该阴极流场板21可较传统型板更薄;因为当流体通过该流体通道213时,本发明的该冷却通道217能够将该阴极流场板21的整个横截面用作散热。因此,在较传统型板相同厚度下,本发明的该阴极流场板21能够提供更多的用于散热的散热区域。It can be understood that the structure in which the fluid passage 213 of the cathode flow field plate 21 communicates with the cooling passage 217 to form a completely penetrating passage (or groove) enables the cooling passage 217 to realize the fuel of the present invention. At the same time as the heat dissipation function of the stack, the external reactive fluid is guided to the fluid passage 213. Further, the cooling passage 217 of the cathode flow field plate 21 realizes the dual functions of gas supply and heat dissipation, and the first end portion 215 of the cathode flow field plate 21 and the two lateral edges 2141 of the cathode plate body 214 are The membrane electrode assembly 10 has a larger contact surface, thereby providing the fuel cell stack of the present invention with better heat dissipation and lowering fan speed sensitivity. Accordingly, as the heat dissipation effect increases and the fan speed sensitivity decreases, the overall volume and weight of the fuel cell can be reduced at the same power output relative to the larger fuel cells that need to be constructed in the prior art. Furthermore, the configuration of the cooling passage 217 of the present invention can reduce the thickness of the cathode flow field plate 21. If the fluid passage of the conventional cathode flow field plate is designed to have a depth of 3 mm, the conventional cathode flow field plate needs to have a thickness of at least 4 mm to maintain the mechanical strength of the cathode flow field plate and ensure heat dissipation efficiency. And if it is the cathode flow field plate 21 of the present invention, when its fluid passage 213 is set to be 3 mm deep The thickness of the cathode flow field plate 21 can be configured to be less than 4 mm. In other words, the cooling passage 217 can be configured as a part of the fluid passage 213 such that the thickness of the cathode flow field plate 21 can be lowered. That is, the cathode flow field plate 21 of the present invention can be thinner than a conventional stencil when achieving the same heat dissipating area; because the cooling passage 217 of the present invention can pass the cathode flow when the fluid passes through the fluid passage 213 The entire cross section of the field plate 21 serves as heat dissipation. Therefore, the cathode flow field plate 21 of the present invention can provide more heat dissipation regions for heat dissipation at the same thickness as conventional panels.
如附图之图3A和图3B所示,该流场板组20的该阳极流场板21′具有一个内侧和一个外侧,其中该阳极流场板21′的内外两侧均为平面侧。该阳极流场板21′的该内侧形成一个通道侧212′和该外侧形成一个平面侧211′,其中该阳极流场板21′的该通道侧212′形成至少一个燃料通道213′,其中该燃料通道213′朝向该膜电极组10以使燃料,如氢燃料,可通过该燃料通道213′被提供给该膜电极组10。该燃料通道213′凹陷在该阳极流场板21′的该通道侧212′。优选地,该阳极流场板21′包括一个阳极板体214′和两个相反的端部,两个第二端部215′,其中该阳极板体214′延伸在两个第二端部215′之间,其中该阳极流场板21′的该阳极板体214′和该第二端部215′形成一个形成在该阳极流场板21′的该通道侧212′的连续密封平面2120′。换句话说,当该燃料电池堆被堆叠时,该流场板组20的该阴极流场板21的该平面侧211和该阳极流场板21′的该通道侧212′能够分别为该膜电极组10提供一个平的支撑,和使该阴极流场板21的该平面侧211和该阳极流场板21′的该通道侧212′能够密封地抵压在该膜电极组10。As shown in Figures 3A and 3B of the accompanying drawings, the anode flow field plate 21' of the flow field plate group 20 has an inner side and an outer side, wherein the inner and outer sides of the anode flow field plate 21' are both planar sides. The inner side of the anode flow field plate 21' forms a channel side 212' and the outer side forms a planar side 211', wherein the channel side 212' of the anode flow field plate 21' forms at least one fuel passage 213', wherein The fuel passage 213' faces the membrane electrode assembly 10 such that a fuel, such as hydrogen fuel, can be supplied to the membrane electrode assembly 10 through the fuel passage 213'. The fuel passage 213' is recessed in the passage side 212' of the anode flow field plate 21'. Preferably, the anode flow field plate 21' includes an anode plate body 214' and two opposite ends, two second ends 215', wherein the anode plate body 214' extends at the two second ends 215 The anode plate body 214' and the second end portion 215' of the anode flow field plate 21' form a continuous sealing plane 2120' formed on the channel side 212' of the anode flow field plate 21'. . In other words, when the fuel cell stack is stacked, the planar side 211 of the cathode flow field plate 21 of the flow field plate group 20 and the channel side 212' of the anode flow field plate 21' can be the film respectively. The electrode assembly 10 provides a flat support, and the planar side 211 of the cathode flow field plate 21 and the channel side 212' of the anode flow field plate 21' are sealingly pressed against the membrane electrode assembly 10.
如附图之图1A、图1B和图4,该流场板组20进一步包括一个密封垫22,其中该密封垫22被设置在该膜电极组10和该阳极流场板21′,其中该密封垫22被设置在该阳极流场板21′的该通道侧212′。1A, 1B and 4, the flow field plate set 20 further includes a gasket 22, wherein the gasket 22 is disposed on the membrane electrode assembly 10 and the anode flow field plate 21', wherein A gasket 22 is disposed on the channel side 212' of the anode flow field plate 21'.
如附图之图2A至图4,当该燃料电池被堆叠时,每相邻两个燃料电池被相互组装在一起,且前一个燃料电池的该阳极流场板21′的该平面侧211′与下一个燃料电池的该阴极流场板21的该通道侧212相耦接,其中前一个燃料电池的该阳极流场板21′的该平面侧211′和下一个燃料电池的该阴极流场板21的该通道侧212形成两个位于两者之间的流体流道2150,其中该流体流道2150分别与该燃料通道213′相连通,以使燃料能够自一个流体流道2150通过该燃料通道213′流向另一个流体流道2150。2A to 4, when the fuel cells are stacked, each adjacent two fuel cells are assembled to each other, and the planar side 211' of the anode flow field plate 21' of the previous fuel cell Coupling with the channel side 212 of the cathode flow field plate 21 of the next fuel cell, wherein the planar side 211' of the anode flow field plate 21' of the previous fuel cell and the cathode flow field of the next fuel cell The channel side 212 of the plate 21 defines two fluid flow channels 2150 therebetween, wherein the fluid flow channels 2150 are in communication with the fuel passages 213', respectively, to enable fuel to pass from the fuel flow path 2150 through the fuel. Channel 213' flows to another fluid flow channel 2150.
如附图之图2A至图4,每个流体流道2150具有一个第一开口21501′和一个第二开口21502′,其中该第一开口21501′和该第二开口21502′均形成在该阳极流场板21′的该第二端部215′,其中该密封垫2150被设置在该阳极流场板21′的该通道侧212′和环绕该流体 流道2150的该第一开口21501′和该第二开口21502′,以防止燃料自该膜电极组10和该阳极流场板21′的该通道侧212′之间的空隙泄漏。如附图之图2A至图4,每个燃料通道213′分别与两个流体流道2150相连通,以允许燃料能够自一个流体流道2150通过该燃料通道213′流向另一个流体流道2150。相应地,该流体流道2150的该第一开口21501′和该第二开口21502′分别是两个分别形成在该阳极流场板21′的两个第二端部215′的穿透型孔和被设置相互对齐。尤其是,每个燃料通道213被设置在该阳极流场板21′的该第二端部215′之间和具有一个蛇形结构,以延长燃料的流经距离,其中每个燃料通道213′的两端分别与该第二开口21502′相连通,如附图之图3B所示。换句话说,燃料被引导穿过该燃料通道213′流动在该阳极流场板21′的该第二端部215′的两个该第二开口21502′之间。可选地,燃料通道213′也可被设置具有其它合适形状。2A to 4, each fluid flow path 2150 has a first opening 21501' and a second opening 21502', wherein the first opening 21501' and the second opening 21502' are both formed at the anode. The second end portion 215' of the flow field plate 21', wherein the gasket 2150 is disposed on the channel side 212' of the anode flow field plate 21' and surrounds the fluid The first opening 21501' of the flow channel 2150 and the second opening 21502' prevent fuel from leaking from the gap between the membrane electrode assembly 10 and the channel side 212' of the anode flow field plate 21'. 2A through 4 of the drawings, each fuel passage 213' is in communication with two fluid flow passages 2150, respectively, to allow fuel to flow from one fluid flow passage 2150 through the fuel passage 213' to the other fluid flow passage 2150. . Correspondingly, the first opening 21501' and the second opening 21502' of the fluid flow path 2150 are respectively two penetrating holes formed in the two second end portions 215' of the anode flow field plate 21'. And are set to align with each other. In particular, each fuel passage 213 is disposed between the second end portion 215' of the anode flow field plate 21' and has a serpentine structure to extend the flow distance of the fuel, wherein each fuel passage 213' The two ends are respectively connected to the second opening 21502', as shown in FIG. 3B of the drawing. In other words, fuel is directed through the fuel passage 213' between the two second openings 21502' of the second end 215' of the anode flow field plate 21'. Alternatively, the fuel passage 213' can also be provided with other suitable shapes.
如附图之图2A至图4,每个流体流道2150形成在该阴极流场板21的该通道侧212,其中该阴极流场板21的每个第一端部215进一步具有一个被设置环绕该流体流道2150的密封槽21502。相应地,该密封槽21502是一个形成在该阴极流场板21的该通道侧212的凹槽以环绕该流体通道2150。该流场板组20进一步包括两个密封圈23,其中该密封圈23被分别设置在该密封槽21502以防止燃料自该阳极流场板21′的该平面侧211′与该阴极流场板21的该通道侧212之间的空隙泄漏。2A to 4, each fluid flow path 2150 is formed on the channel side 212 of the cathode flow field plate 21, wherein each first end portion 215 of the cathode flow field plate 21 further has a set A sealing groove 21502 surrounding the fluid flow path 2150. Correspondingly, the sealing groove 21502 is a groove formed in the channel side 212 of the cathode flow field plate 21 to surround the fluid channel 2150. The flow field plate set 20 further includes two sealing rings 23, wherein the sealing ring 23 is respectively disposed in the sealing groove 21502 to prevent fuel from the planar side 211' of the anode flow field plate 21' and the cathode flow field plate. The gap between the channel sides 212 of 21 leaks.
如附图之图2A至图4,每个流体流道2150进一步具有一个形成在该阴极流场板21的该第一端部215的第三开口21501,其中该第三开口2501穿过该阴极流场板21。值得注意的是,当一组燃料电池被相互堆叠在一起以形成一个燃料电池堆时,该阴极流场板21的该第一端部215的该第三开口21501和相应的该阳极流场板21′的该第二端部215′的该第二开口21502′形成一个燃料流道200,从而使得氢燃料可通过该燃料电池堆的该燃料流道200被提供。2A to 4, each fluid flow path 2150 further has a third opening 21501 formed in the first end portion 215 of the cathode flow field plate 21, wherein the third opening 2501 passes through the cathode Flow field plate 21. It is noted that when a group of fuel cells are stacked on each other to form a fuel cell stack, the third opening 21501 of the first end portion 215 of the cathode flow field plate 21 and the corresponding anode flow field plate The second opening 21502' of the second end 215' of 21' forms a fuel flow passage 200 such that hydrogen fuel can be supplied through the fuel flow passage 200 of the fuel cell stack.
可选地,该流体流道2150分别形成在该阳极流场板21′的该平面侧211′和两个密封槽21502被设置分别环绕该流体流道2150,其中该流场板组20进一步包括两个密封圈23,其中该密封圈23被分别设置在该密封槽21502以防止燃料自该阳极流场板21′的该平面侧211′与该阴极流场板21的该通道侧212之间的空隙泄漏。Optionally, the fluid flow channel 2150 is formed on the planar side 211' of the anode flow field plate 21' and the two sealing grooves 21502 are respectively disposed around the fluid flow channel 2150, wherein the flow field plate group 20 further includes Two seal rings 23, wherein the seal rings 23 are respectively disposed in the seal groove 21502 to prevent fuel from between the plane side 211' of the anode flow field plate 21' and the channel side 212 of the cathode flow field plate 21 The gap leaks.
如附图之图3B所示,依本发明较佳实施例的该燃料电池堆的该电池单元的该密封垫22为一空心结构以实现密封部分位于该阳极流场板21′的该通道侧212′的周缘。换言之,该密封垫22为一中空结构以实现流体,如气体,从中通过。该密封垫22进一步被设置与该阳极流场板21′的通道侧212′相匹配的尺寸和形状。如图3B所示,该密封垫22的密封 部分分别被设置在该阳极流场板21′的该第二端部215′和该阳极板体214′,以形成一个密闭环境用于氢流动。可以理解的是,该燃料通道213′不被该密封垫22遮盖。As shown in FIG. 3B of the accompanying drawings, the gasket 22 of the battery cell of the fuel cell stack according to the preferred embodiment of the present invention has a hollow structure to achieve a sealing portion on the channel side of the anode flow field plate 21'. The circumference of 212'. In other words, the gasket 22 is a hollow structure to allow a fluid, such as a gas, to pass therethrough. The gasket 22 is further sized and shaped to match the channel side 212' of the anode flow field plate 21'. Seal of the gasket 22 as shown in FIG. 3B Portions are respectively disposed at the second end portion 215' of the anode flow field plate 21' and the anode plate body 214' to form a closed environment for hydrogen flow. It will be appreciated that the fuel passage 213' is not covered by the gasket 22.
附图之图3B也显示了本发明优选实施方式的燃料电池堆设计,即无论采用何种密封方式,例如粘合性垫,则该粘合性垫处于挤压状态。值得一提的是,由于该膜电极组10与该阴阳两极流场板21、21′的平面侧211、212′之间通过该密封垫22密封,形成了一个密闭环境用于氢流动,从而使得该阳极流场板21′的通道侧212′被密封和以防止氢渗漏。相应地,本发明的该密封垫22可为一环边垫圈或粘合性垫圈。该密封垫22优选为由柔性材料制成的密封垫结构,其被设置在该阳极流场板21′的该通道侧212′,以防止电池堆工作时,发生氢气渗漏。因此,该流场板组20仅需一个密封垫22即可实现其阴极流场板21的平面侧211和阳极流场板21′的通道侧212′之间的密封。Figure 3B of the accompanying drawings also shows a fuel cell stack design in accordance with a preferred embodiment of the present invention, i.e., regardless of the type of sealing employed, such as an adhesive pad, the adhesive pad is in a compressed state. It is worth mentioning that since the membrane electrode assembly 10 and the planar sides 211, 212' of the cathode and cathode flow field plates 21, 21' are sealed by the gasket 22, a closed environment is formed for hydrogen flow, thereby The channel side 212' of the anode flow field plate 21' is sealed and protected from hydrogen leakage. Accordingly, the gasket 22 of the present invention can be a loop gasket or an adhesive gasket. The gasket 22 is preferably a gasket structure made of a flexible material disposed on the channel side 212' of the anode flow field plate 21' to prevent hydrogen leakage when the stack is in operation. Therefore, the flow field plate assembly 20 requires only one gasket 22 to achieve a seal between the planar side 211 of the cathode flow field plate 21 and the channel side 212' of the anode flow field plate 21'.
当该流场板(阴极流场板21)21作为燃料电池的阴极流场板使用时,该阴极流场板21的平面侧211被安装至该膜电极组10。该质子交换薄膜燃料电池配置为向大气中开放,因此,氧化剂,如空气(或氧气)通过该阴极流场板21被吹入该流体通道213。该冷却通道217的构造提升了空气冷却效率,因为热量通过该冷却通道217被消散和分离。该冷却通道217增强了散热效果和能够使该阴极流场板21相较于传统型更薄。更薄且轻的燃料电池堆的能够使其相较于现有技术更具便携性。When the flow field plate (cathode flow field plate 21) 21 is used as a cathode flow field plate of a fuel cell, the planar side 211 of the cathode flow field plate 21 is mounted to the membrane electrode assembly 10. The proton exchange membrane fuel cell is configured to be open to the atmosphere, and therefore an oxidant such as air (or oxygen) is blown into the fluid passage 213 through the cathode flow field plate 21. The configuration of the cooling passage 217 enhances air cooling efficiency because heat is dissipated and separated through the cooling passage 217. The cooling passage 217 enhances the heat dissipation effect and enables the cathode flow field plate 21 to be thinner than the conventional type. A thinner and lighter fuel cell stack can make it more portable than the prior art.
特别地,该冷却通道217自该阴极流场板21成型以降低薄膜含水量对风扇转速的敏感度。该冷却通道217相对每个流体通道213成型。当气体穿过该阴极流场板21的该冷却通道217和该流体通道213时,气流将仅通过该冷却通道217从该阴极流场板21带走热量。该冷却通道217和该流体通道213将保持该膜电极组10的水含量,因为通过该冷却通道217的散热气流并不与该膜电极组10直接接触。因此,当风扇转速增快或减慢时,仅有部分气流直接影响该膜电极组10水含量,但所有气流均有冷却效果。换言之,该燃料电池的电池电压相对风扇转速变得更低敏感度。In particular, the cooling passage 217 is molded from the cathode flow field plate 21 to reduce the sensitivity of the film moisture content to the fan speed. The cooling passage 217 is formed with respect to each fluid passage 213. As the gas passes through the cooling passage 217 and the fluid passage 213 of the cathode flow field plate 21, the gas flow will only carry heat away from the cathode flow field plate 21 through the cooling passage 217. The cooling passage 217 and the fluid passage 213 will maintain the water content of the membrane electrode assembly 10 because the heat dissipation gas flow through the cooling passage 217 is not in direct contact with the membrane electrode assembly 10. Therefore, when the fan speed increases or slows down, only part of the airflow directly affects the water content of the membrane electrode assembly 10, but all airflows have a cooling effect. In other words, the battery voltage of the fuel cell becomes less sensitive to the fan speed.
此外,本发明提供的该阴极流场板21可同样提供燃料电池的热和水管理。相应地,该膜电极组10需含水量较高以维持低内阻。当气体吹入和通过该流体通道213时,其仅经该冷却通道217冷却,该阴极流场板21并不加速水蒸发,以防止该膜电极组10水含量降低。Furthermore, the cathode flow field plate 21 provided by the present invention can likewise provide heat and water management for the fuel cell. Accordingly, the membrane electrode assembly 10 requires a high water content to maintain a low internal resistance. When the gas is blown into and through the fluid passage 213, it is cooled only by the cooling passage 217, and the cathode flow field plate 21 does not accelerate the evaporation of water to prevent the water content of the membrane electrode assembly 10 from being lowered.
值得一提的是,依本发明较佳实施例的该明流场板组20可使燃料电池堆之间的差异更小。换句话说,使用本发明流场板组20的燃料电池之间具有均一性。因此,本发明提供的燃料电池堆因能够采用更高氢压力而更容易实现电池电压的均一性。 It is worth mentioning that the bright flow field plate set 20 according to a preferred embodiment of the invention can make the difference between the fuel cell stacks smaller. In other words, the fuel cells using the flow field plate set 20 of the present invention have uniformity between them. Therefore, the fuel cell stack provided by the present invention can more easily achieve the uniformity of the battery voltage by being able to adopt a higher hydrogen pressure.
附图之图7A至图7C阐明了依本发明较佳实施例的该燃料电池堆的该流场板组20的该阴极流场板21的一种可选实施,其中该流场板组20A包括一个阴极流场板21A和一个阳极流场板21′,其中该阴极流场板21A具有一个平面侧211A和一个通道侧212A,并包括一个阴极板体214A和两个相反的端部,两个第一端部215A,其中该阴极板体214A延伸在该第一端部215A之间,其中该阴极板体214A包括两个横向边缘2141A和一组引导墙216A,其中该引导墙216A被分别相隔开地设置在该横向边缘2141A之间,其中每两个相邻的216A形成一个位于两者之间的流体通道213A,和每个引导墙216A形成一个冷却通道217A,其中该冷却通道217A形成在该阴极流场板21的该通道侧212A,其中每个该冷却通道217A自该阴极板体214A的一个横向边缘2141A延伸至另一个横向边缘2141A,以使流体能够流过该冷却通道217A。优选地,该阴极板体21A的每个第一端部215A形成一个流体流道2150A,其中该流体通道2150A具有一个第三开口21501A和一个密封槽21502A。7A through 7C illustrate an alternate implementation of the cathode flow field plate 21 of the flow field plate set 20 of the fuel cell stack in accordance with a preferred embodiment of the present invention, wherein the flow field plate set 20A A cathode flow field plate 21A and an anode flow field plate 21' are included, wherein the cathode flow field plate 21A has a planar side 211A and a channel side 212A, and includes a cathode plate body 214A and two opposite ends, two First end portions 215A, wherein the cathode plate body 214A extends between the first end portions 215A, wherein the cathode plate body 214A includes two lateral edges 2141A and a set of guiding walls 216A, wherein the guiding walls 216A are respectively Separably disposed between the lateral edges 2141A, wherein each two adjacent 216A form a fluid passage 213A therebetween, and each guide wall 216A forms a cooling passage 217A, wherein the cooling passage 217A Formed on the channel side 212A of the cathode flow field plate 21, wherein each of the cooling channels 217A extends from one lateral edge 2141A of the cathode plate body 214A to the other lateral edge 2141A to enable fluid to flow through the cooling channel 217A . Preferably, each of the first end portions 215A of the cathode plate body 21A forms a fluid flow path 2150A, wherein the fluid passage 2150A has a third opening 21501A and a seal groove 21502A.
附图之图8A至图8F阐明了依本发明较佳实施例的该燃料电池堆的该流场板组20的另一种可选实施,其中该流场板组20C包括至少两个流场板21C,其中每个流场板21C包括一个阴极板体211C、一个阳极板体212C和一组引导墙213C,其中该阴极板体211C形成一组相互隔开的第一流体槽2110C,其中该引导墙213C被相隔开地设置在该阴极板体211C和该阳极板体212C之间,从而使得每相邻两个引导墙213C形成一个位于两者之间的第二流体槽2130C,其中该阴极板体211C的该第一流体槽2110C被设置分别与该第二流体槽2130C相对齐和相连通,从而使得每个第一流体槽2110C与相应的第二流体槽2130C形成一个连续的流体通道214C,其中该流体通道214C具有一个第一通道开口2141C、一个第二通道开口2142C和一个第三通道开口2143C,其中该流体通道214C的该第三通道开口2143C被设置朝向该膜电极组10,从而使得该流体通道214C允许反应活性物质流体,如空气、氧气等流动在该流体通道214C的该第一通道开口2141C和该第二通道开口2142C之间,并通过该第三通道开口2143C被提供给该膜电极组10。优选地,该第一流体槽2110C的长度大于该第二流体槽2130C的长度,和该第一流体槽2110C的宽度小于该第二流体槽2130C的宽度。8A through 8F illustrate another alternative implementation of the flow field plate set 20 of the fuel cell stack in accordance with a preferred embodiment of the present invention, wherein the flow field plate set 20C includes at least two flow fields The plate 21C, wherein each flow field plate 21C includes a cathode plate body 211C, an anode plate body 212C and a set of guide walls 213C, wherein the cathode plate body 211C forms a set of first fluid grooves 2110C spaced apart from each other, wherein The guiding wall 213C is disposed between the cathode plate body 211C and the anode plate body 212C so as to be spaced apart such that each adjacent two guiding walls 213C form a second fluid groove 2130C therebetween. The first fluid groove 2110C of the cathode plate body 211C is disposed to be in parallel with and in communication with the second fluid groove 2130C, respectively, such that each of the first fluid grooves 2110C forms a continuous fluid passage with the corresponding second fluid groove 2130C. 214C, wherein the fluid passage 214C has a first passage opening 2141C, a second passage opening 2142C, and a third passage opening 2143C, wherein the third passage opening 2143C of the fluid passage 214C is disposed toward the membrane electrode assembly 10, thereby The fluid passage 214C is allowed to allow a reactive material fluid such as air, oxygen, or the like to flow between the first passage opening 2141C of the fluid passage 214C and the second passage opening 2142C, and is supplied to the third passage opening 2143C through the third passage opening 2143C The membrane electrode assembly 10. Preferably, the length of the first fluid groove 2110C is greater than the length of the second fluid groove 2130C, and the width of the first fluid groove 2110C is smaller than the width of the second fluid groove 2130C.
如附图之图8A至图8F所示,每个流场板21C具有一个第一通道侧215C和一个第二通道侧216C,其中该阴极板体211C的该第一通道侧215C形成在该阴极板体211C的一个外侧,该阳极板体212C的该第二通道侧216C形成在该阳极板体212C的一个外侧,其中该流场板21C具有至少一个被设置在该流场板21C的该第二通道侧216C的燃料通道 217C,和该流场板21C的该第二通道侧216C被设置朝向该膜电极组10,从而使得燃料,如氢气,可通过该燃料通道217C被提供给该膜电极组10。换句话说,该阴极板体211C的该第一流体槽2110C形成在该阴极板体211C的该外侧,该阳极板体212C的该燃料通道217C形成在该阳极板体212C的该外侧。As shown in FIGS. 8A to 8F of the drawings, each flow field plate 21C has a first channel side 215C and a second channel side 216C, wherein the first channel side 215C of the cathode plate body 211C is formed at the cathode. An outer side of the plate body 211C, the second channel side 216C of the anode plate body 212C is formed on an outer side of the anode plate body 212C, wherein the flow field plate 21C has at least one portion disposed on the flow field plate 21C Two-channel side 216C fuel passage 217C, and the second channel side 216C of the flow field plate 21C are disposed toward the membrane electrode assembly 10 such that a fuel, such as hydrogen, can be supplied to the membrane electrode assembly 10 through the fuel passage 217C. In other words, the first fluid groove 2110C of the cathode plate body 211C is formed on the outer side of the cathode plate body 211C, and the fuel passage 217C of the anode plate body 212C is formed on the outer side of the anode plate body 212C.
如附图之图8A所示,依本发明较佳实施例的该燃料电池的该流场板组20C包括至少两个流场板21C,其中每个膜电极组10被设置在相邻两个流场板中的前一个流场板21C的该第二通道侧216C与后一个流场板21C的该第一通道侧215C之间。换句话说,相邻两个流场板中的前一个流场板21C的该第二通道侧216C、后一个流场板21C的该第一通道侧215C和该膜电极组10形成一个电池单元。As shown in FIG. 8A of the accompanying drawings, the flow field plate group 20C of the fuel cell according to the preferred embodiment of the present invention includes at least two flow field plates 21C, wherein each of the membrane electrode groups 10 is disposed adjacent to two The second channel side 216C of the previous flow field plate 21C in the flow field plate is between the first channel side 215C of the subsequent flow field plate 21C. In other words, the second channel side 216C of the previous one of the adjacent flow field plates 21C, the first channel side 215C of the latter flow field plate 21C, and the membrane electrode assembly 10 form a battery cell .
如附图之图8B至图8F所示,该流场板组20C的每个流场板21C的该引导墙213C被设置在该阳极板体212C的一个内侧,并自该阳极板体212C的该内侧延伸。优选地,该流场板21C的该引导墙213C与该阳极板体212C一体成型。更优选地,该流场板组20C的该流场板21C的该阴极板体211C被可拆卸地设置在该引导墙213C。As shown in FIG. 8B to FIG. 8F of the drawing, the guide wall 213C of each flow field plate 21C of the flow field plate group 20C is disposed on one inner side of the anode plate body 212C, and from the anode plate body 212C. This inner side extends. Preferably, the guiding wall 213C of the flow field plate 21C is integrally formed with the anode plate body 212C. More preferably, the cathode plate body 211C of the flow field plate 21C of the flow field plate group 20C is detachably disposed at the guide wall 213C.
如附图之图8A至图8F所示,该流场板组20C的该流场板21C的该阴极板体211C具有一个形成在该阴极板体211C的一个内侧的容纳槽218C,其中该容纳槽218C的形状和大小依该流场板21C的该引导墙213C被设置,以能够将该流场板21C的该引导墙213C容纳于其内,并使该引导墙213C形成的该第二流体槽2130C分别与该阴极板体211C的该第一流体槽2110C相对齐和相连通,从而形成该流体通道214C。更优选地,该容纳槽218C的深度与该流场板21C的该引导墙213C的高度相同,从而使得该流场板21C的该引导墙213C能够被相适配地容纳在该阴极板体211C的该容纳槽218C。As shown in FIGS. 8A to 8F of the accompanying drawings, the cathode plate body 211C of the flow field plate 21C of the flow field plate group 20C has a receiving groove 218C formed on one inner side of the cathode plate body 211C, wherein the receiving portion 218C is accommodated therein. The shape and size of the groove 218C are set according to the guide wall 213C of the flow field plate 21C to accommodate the guide wall 213C of the flow field plate 21C therein, and the second fluid formed by the guide wall 213C The grooves 2130C are respectively in line with and in communication with the first fluid groove 2110C of the cathode plate body 211C, thereby forming the fluid passage 214C. More preferably, the depth of the receiving groove 218C is the same as the height of the guiding wall 213C of the flow field plate 21C, so that the guiding wall 213C of the flow field plate 21C can be accommodated in the cathode plate body 211C. The receiving groove 218C.
如附图之图8A至图8F所示,该流场板组20C的该流场板21C的该阴极板体211C包括两个相反的端部,两个第一端部2111C、两个分别延伸在该第一端部2111C之间的第一横向边缘2112C和一个纵向地延伸在该第一横向边缘2112C之间的第一形成部2113C,其中该第一形成部2113C形成延伸在该第一横向边缘2112C之间的第一流体槽2110C,其中该阴极板体211C的该第一端部2111C和该第一横向边缘2112C在该流场板21C的该第一通道侧215C形成一个连续密封平面2150C,其中该连续密封平面2150C被设置环绕该阴极板体211C的该第一形成部2113C;该流场板21C的该阳极板体212C包括两个相反的端部,两个第二端部2121C、两个分别延伸在该第二端部2121C之间的第二横向边缘2122C和一个纵向地延伸在该第二横向边缘2122C之间的第二形成部2123C,其中该第二形成部2123C形成延伸在该第二端部2121C之间的燃料通道217C,其中该阳极板 体212C的该第二端部2121C和该第二横向边缘2122C在该流场板21C的该第二通道侧216C形成一个连续密封平面2160C,其中该连续密封平面2160C被设置环绕该阳极板体212C的该第二形成部2123C,从而使得当该燃料电池堆被堆叠时,该流场板21C的该第一通道侧215C和该第二通道侧216C能够分别为该膜电极组10提供一个平的支撑,和使该流场板21C的该第一通道侧215C和该第二通道侧216C能够密封地抵压在该膜电极组10。As shown in FIGS. 8A to 8F of the accompanying drawings, the cathode plate body 211C of the flow field plate 21C of the flow field plate group 20C includes two opposite end portions, and the two first end portions 2111C and the two extend respectively. a first lateral edge 2112C between the first end portion 2111C and a first forming portion 2113C extending longitudinally between the first lateral edge 2112C, wherein the first forming portion 2113C is formed to extend in the first lateral direction a first fluid groove 2110C between the edges 2112C, wherein the first end portion 2111C of the cathode plate body 211C and the first lateral edge 2112C form a continuous sealing plane 2150C on the first channel side 215C of the flow field plate 21C Wherein the continuous sealing plane 2150C is disposed around the first forming portion 2113C of the cathode plate body 211C; the anode plate body 212C of the flow field plate 21C includes two opposite ends, two second ends 2121C, Two second lateral edges 2122C extending between the second ends 2121C and a second forming portion 2123C extending longitudinally between the second lateral edges 2122C, wherein the second forming portion 2123C is formed to extend over Fuel passage 217 between the second ends 2121C C, wherein the anode plate The second end portion 2121C of the body 212C and the second lateral edge 2122C form a continuous sealing plane 2160C on the second passage side 216C of the flow field plate 21C, wherein the continuous sealing plane 2160C is disposed around the anode plate body 212C. The second forming portion 2123C, such that the first channel side 215C and the second channel side 216C of the flow field plate 21C can provide a flat level for the membrane electrode assembly 10 when the fuel cell stack is stacked The first channel side 215C and the second channel side 216C of the flow field plate 21C are supported and sealed against the membrane electrode assembly 10.
可以理解的是,位于该流场板21C的该阴极板体211C的该第一流体槽2110C与该第二流体槽2130C相连通以形成一个完全穿透型流体通道214C(或槽)的这种结构可使该第二流体槽2130C实现本发明燃料电池堆的散热功能的同时,起到将外部反应活性流体引导至该第一流体槽2110C的作用。进一步地,该流场板21C的该第二流体槽2130C实现供气和散热的双重功能,且该阴极板体211C的该第一端部2111C和该横向边缘2112C与该膜电极组10具有一个更大的接触面,从而使本发明燃料电池堆具有更好的散热效果和降低风扇转速敏感度。相应地,随着散热效应的提升和风扇转速敏感度的降低,在相同功率输出下,相对于现有技术需要构建的更大型的燃料电池,该燃料电池的整体体积和重量均能够被降低。此外,本发明该流体通道214C的构造可降低阴极板体211C(或阴极流场板)的厚度。如果传统型阴极流场板的流体通道设计为3mm深度,则传统型阴极流场板需至少4mm厚度,以保持阴极流场板的机械强度和确保散热效率。而如果是本发明阴极板体211C,则当其流体通道214C被设置为3mm深度时,该阴极板体211C的厚度则可配置为小于4mm。换言之,该第二流体槽2130C可作为该流体通道214C的一部分的配置,使得该阴极板体211C的厚度可被降低。也就是说,在实现相同散热面积时,本发明的该阴极板体211C可较传统型阴极流场板更薄;因为当流体通过该流体通道214C时,本发明的该第二流体槽2130C能够将该阴极板体211C的整个横截面用作散热。因此,在较传统型板相同厚度下,本发明的该阴极板体211C能够提供更多的用于散热的散热区域。It can be understood that the first fluid tank 2110C of the cathode plate body 211C of the flow field plate 21C communicates with the second fluid tank 2130C to form a fully penetrating fluid passage 214C (or groove). The structure allows the second fluid tank 2130C to function to direct the external reactive fluid to the first fluid tank 2110C while achieving the heat dissipation function of the fuel cell stack of the present invention. Further, the second fluid groove 2130C of the flow field plate 21C realizes the dual functions of gas supply and heat dissipation, and the first end portion 2111C and the lateral edge 2112C of the cathode plate body 211C and the membrane electrode assembly 10 have one The larger contact surface allows the fuel cell stack of the present invention to have better heat dissipation and reduce fan speed sensitivity. Accordingly, as the heat dissipation effect increases and the fan speed sensitivity decreases, the overall volume and weight of the fuel cell can be reduced at the same power output relative to the larger fuel cells that need to be constructed in the prior art. Furthermore, the configuration of the fluid passage 214C of the present invention can reduce the thickness of the cathode plate body 211C (or the cathode flow field plate). If the fluid passage of the conventional cathode flow field plate is designed to have a depth of 3 mm, the conventional cathode flow field plate needs to have a thickness of at least 4 mm to maintain the mechanical strength of the cathode flow field plate and ensure heat dissipation efficiency. On the other hand, in the case of the cathode plate body 211C of the present invention, when the fluid passage 214C is set to a depth of 3 mm, the thickness of the cathode plate body 211C can be configured to be less than 4 mm. In other words, the second fluid tank 2130C can be configured as part of the fluid passage 214C such that the thickness of the cathode plate body 211C can be lowered. That is, the cathode plate body 211C of the present invention can be thinner than the conventional cathode flow field plate when the same heat dissipation area is realized; because the second fluid groove 2130C of the present invention can be used when the fluid passes through the fluid passage 214C The entire cross section of the cathode plate body 211C is used as heat dissipation. Therefore, the cathode plate body 211C of the present invention can provide more heat dissipation regions for heat dissipation at the same thickness as conventional panels.
如附图之图8A至图8F所示,该流场板组20C的该流场板21C的该阴极板体211C的每个第一端部2111C具有一个第一连通开口21110C,该阳极板体212C的每个第二端部2121C具有一个第二连通开口21210C,其中该阴极板体211C的该第一端部2111C的该第一连通开口21110C分别与相对应的该阳极板体212C的该第二端部2121C的该第二连通开口21210C相连通和形成一个燃料流道200C,其中该流场板21C的每个燃料通道217C的两端分别与该燃料流道200C相连通,从而使得氢燃料可通过该燃料电池堆的该 流场板组20C的该流场板21C的该燃料流道200C被提供。As shown in FIG. 8A to FIG. 8F of the drawing, each first end portion 2111C of the cathode plate body 211C of the flow field plate 21C of the flow field plate group 20C has a first communication opening 21110C, and the anode plate body Each of the second ends 2121C of the 212C has a second communication opening 21210C, wherein the first communication opening 21110C of the first end portion 2111C of the cathode plate body 211C and the corresponding anode plate body 212C are respectively The second communication opening 21210C of the two end portions 2121C communicates with each other and forms a fuel flow path 200C, wherein both ends of each of the fuel passages 217C of the flow field plate 21C are respectively communicated with the fuel flow path 200C, thereby causing hydrogen fuel Passing the fuel cell stack The fuel flow path 200C of the flow field plate 21C of the flow field plate group 20C is supplied.
如附图之图8A至图8F所示,该流场板组20C的相邻两个流场板21C之间的密封可通过一个密封垫22C而被实现,其中该密封垫22C为一空心结构,且该密封垫22C的密封部分被设置在前一个流场板21C的该阳极板体212C的该外侧的周缘。换言之,该密封垫22C为一中空结构以实现流体,如气体,从中通过。该密封垫22C进一步被设置与该阳极板体212C的该外侧相匹配的尺寸和形状。如图8A至图8F所示,该密封垫22C分别被设置在两个相邻流场板21C的前一个流场板21C的该阳极板体212C的该外侧,其中该密封垫22C为一空心结构,且该密封垫22C的密封部分被设置在前一个流场板21C的该阳极板体212C和后一个流场板21C的该阴极板体211C之间和该膜电极组10的周缘被设置在该密封垫22C的密封部分与前一个流场板21C的该阳极板体212C之间,从而使得前一个流场板21C的该阳极板体212C、后一个流场板21C的该阴极板体211C和该膜电极组10形成一个密封空间,以用于燃料流动。进一步地,该密封垫22C的两端被分别设置在前一个流场板21C的该阳极板体212C的该端部和相应的后一个流场板21C的该阴极流场板211C的该端部之间,其中该密封垫22C被设置分别围绕前一个流场板21C的该阳极板体212C的两个第一连通开口21110C和后一个流场板21C的该阴极流场板211C的两个第二连通开口21210C,从而使得当该燃料电池被组装和该密封垫22C被挤压在两个流场板21C之间时,前一个流场板21C的该阳极板体212C和后一个流场板21C的该阴极板体211C被密封地相互堆叠在一起,以防止燃料自前一个流场板21C的该阳极板体211C和后一个流场板21C的该阴极板体211C之间的空隙泄漏。可以理解的是,该燃料通道217C不被该密封垫22C遮盖。优选地,该密封垫22C进一步被设置在该阴极板体211C的两个端部和围绕该阳极板体212C的该燃料通道217C,以形成一个密封空间用于氢流动。换句话说,该燃料通道217C不被该密封垫22C遮盖。As shown in FIGS. 8A to 8F of the accompanying drawings, the seal between the adjacent two flow field plates 21C of the flow field plate group 20C can be realized by a gasket 22C, wherein the gasket 22C is a hollow structure. And the sealing portion of the gasket 22C is disposed on the outer circumference of the anode plate body 212C of the previous flow field plate 21C. In other words, the gasket 22C is a hollow structure to allow a fluid, such as a gas, to pass therethrough. The gasket 22C is further provided in a size and shape that matches the outer side of the anode plate body 212C. As shown in FIG. 8A to FIG. 8F, the gaskets 22C are respectively disposed on the outer side of the anode plate body 212C of the previous flow field plate 21C of two adjacent flow field plates 21C, wherein the gasket 22C is a hollow. Structure, and a sealing portion of the gasket 22C is disposed between the anode plate body 212C of the previous flow field plate 21C and the cathode plate body 211C of the subsequent flow field plate 21C and the periphery of the membrane electrode group 10 is disposed Between the sealing portion of the gasket 22C and the anode plate body 212C of the previous flow field plate 21C, so that the anode plate body 212C of the previous flow field plate 21C, the cathode plate body of the latter flow field plate 21C 211C and the membrane electrode assembly 10 form a sealed space for fuel flow. Further, both ends of the gasket 22C are respectively disposed at the end of the anode plate body 212C of the previous flow field plate 21C and the end portion of the cathode flow field plate 211C of the corresponding subsequent flow field plate 21C. Between the two seals 22C being disposed around the two first communication openings 21110C of the anode plate body 212C of the previous flow field plate 21C and the second flow communication plate 211C of the latter flow field plate 21C The second opening 2110C is such that when the fuel cell is assembled and the gasket 22C is squeezed between the two flow field plates 21C, the anode plate body 212C and the latter flow field plate of the previous flow field plate 21C The cathode plates 211C of 21C are sealedly stacked on each other to prevent leakage of fuel from the gap between the anode plate body 211C of the previous flow field plate 21C and the cathode plate body 211C of the latter flow field plate 21C. It will be appreciated that the fuel passage 217C is not covered by the gasket 22C. Preferably, the gasket 22C is further disposed at both ends of the cathode plate body 211C and the fuel passage 217C surrounding the anode plate body 212C to form a sealed space for hydrogen flow. In other words, the fuel passage 217C is not covered by the gasket 22C.
如附图之图8B所示,该流场板组20C的该流场板21C的该阴极板体211C的该第一端部2111C被分别地和密封地设置在该阳极板体212C的该第二端部2121C,以防止氢燃料通过该流场板组20C的该流场板21C的该阴极板体211C的该第一端部2111C和相应的该阳极板体212C的该第二端部2121C之间的空隙泄漏。因此,该流场板组20C的该流场板21C的该阴极板体211C的该第一端部2111C和相应的该阳极板体212C的该第二端部2121C被密封地相互耦接在一起,以防止该阴极板体211C的该第一端部2111C和相应的该阳极板体212C的该第二端部2121C形成位于两者之间的与该燃料流道200C相连通的空隙的形成。该流场板21C的该阴极板体211C的该第一端部2111C和相应的该阳极 板体212C的该第二端部2121C之间的密封可通过一个被设置围绕该阴极板体211C的该第一端部2111C的该第一连通开口21110C(或围绕相应的该阳极板体212C的该第二端部2121C的该第二连通开口21210C)的密封环或密封垫23C而被实现。在另一些实施例中,该阴极板体211C的该第一端部2111C和相应的该阳极板体212C的该第二端部2121C之间的密封通过将该阴极板体211C的该第一端部2111C和相应的该阳极板体212C的该第二端部2121C紧密贴合在一起而被实现。在其它实施例中,该阴极板体211C的该第一端部2111C和相应的该阳极板体212C的该第二端部2121C之间的密封通过使用胶水或粘附剂将该阴极板体211C的该第一端部2111C和相应的该阳极板体212C的该第二端部2121C粘附在一起而被实现。As shown in FIG. 8B of the drawing, the first end portion 2111C of the cathode plate body 211C of the flow field plate 21C of the flow field plate group 20C is separately and sealingly disposed on the anode plate body 212C. The second end portion 2121C prevents the hydrogen fuel from passing through the first end portion 2111C of the cathode plate body 211C of the flow field plate 21C of the flow field plate group 20C and the corresponding second end portion 2121C of the anode plate body 212C. The gap between the leaks. Therefore, the first end portion 2111C of the cathode plate body 211C of the flow field plate 21C of the flow field plate group 20C and the second end portion 2121C of the corresponding anode plate body 212C are sealingly coupled to each other. The first end portion 2111C of the cathode plate body 211C and the second end portion 2121C of the corresponding anode plate body 212C are formed to form a gap between the two communicating with the fuel flow path 200C. The first end portion 2111C of the cathode plate body 211C of the flow field plate 21C and the corresponding anode The seal between the second end portion 2121C of the plate body 212C may pass through the first communication opening 21110C (or around the corresponding anode plate body 212C) disposed around the first end portion 2111C of the cathode plate body 211C. The seal ring or gasket 23C of the second communication opening 21210C) of the second end portion 2121C is realized. In other embodiments, the sealing between the first end portion 2111C of the cathode plate body 211C and the second end portion 1211C of the corresponding anode plate body 212C passes through the first end of the cathode plate body 211C. The portion 2111C and the corresponding second end portion 2121C of the anode plate body 212C are brought into close contact with each other to be realized. In other embodiments, the sealing between the first end portion 2111C of the cathode plate body 211C and the second end portion 2121C of the corresponding anode plate body 212C is performed by using a glue or an adhesive to the cathode plate body 211C. The first end portion 2111C and the second end portion 1211C of the corresponding anode plate body 212C are adhered together to be realized.
附图之图9A至图9F阐明了依本发明较佳实施例的该燃料电池堆的该流场板组20D的另一种可选实施,其中该流场板组20D包括至少两个流场板21D,其中每个流场板21D包括一个流场板体211D、一组第一引导墙212D和一组第二引导墙213D,其中该流场板体211D具有一个阴极侧2111D和一个阳极侧2112D,其中该流场板体211D具有至少一个被设置在该阳极侧2112D的燃料通道215D,其中该第一引导墙212D被相隔开地设置在该流场板体211D的该阴极侧2111D,该第二引导墙213D分别自该第一引导墙212D延伸,从而使得每相邻两个第一引导墙212D形成一个位于两者之间的第一流体通道216D,和相应的相邻两个第二引导墙213D形成一个位于两者之间的第二流体通道217D,其中该第一流体通道216D与该第二流体通道217D相连通,其中每个第一流体通道216D具有两个第一通道开口2161D,每个第二流体通道217D具有一个第二通道开口2171D,其中该第二流体通道217D的该第二通道开口2171D被设置朝向前一个膜电极组10,从而使得该第一流体通道216D允许反应活性物质,如空气或氧气等能够流动在该第一流体通道216D和使反应活性物质能够通过该第二流体通道217D的该第二通道开口2171D被提供给该膜电极组10;其中该流场板体211D的该燃料通道215D被设置朝向后一个膜电极组10,从而使得氢燃料能够通过该燃料通道215D被提供给该膜电极组10。Figures 9A through 9F illustrate another alternative implementation of the flow field plate set 20D of the fuel cell stack in accordance with a preferred embodiment of the present invention, wherein the flow field plate set 20D includes at least two flow fields The plate 21D, wherein each flow field plate 21D includes a flow field plate 211D, a set of first guide walls 212D, and a set of second guide walls 213D, wherein the flow field plate 211D has a cathode side 2111D and an anode side 2112D, wherein the flow field plate 211D has at least one fuel passage 215D disposed on the anode side 2112D, wherein the first guide wall 212D is spaced apart from the cathode side 2111D of the flow field plate 211D, The second guiding walls 213D respectively extend from the first guiding wall 212D such that each adjacent two guiding walls 212D form a first fluid passage 216D between the two, and corresponding two adjacent The second guide wall 213D forms a second fluid passage 217D therebetween, wherein the first fluid passage 216D is in communication with the second fluid passage 217D, wherein each first fluid passage 216D has two first passage openings 2161D, each second fluid channel 217D a second passage opening 2171D, wherein the second passage opening 2171D of the second fluid passage 217D is disposed toward the previous membrane electrode assembly 10 such that the first fluid passage 216D allows reactive substances such as air or oxygen to be capable of The first fluid passage 216D and the second passage opening 2171D enabling the reactive material to pass through the second fluid passage 217D are supplied to the membrane electrode assembly 10; wherein the fuel passage 215D of the flow field plate 211D is The latter is directed toward the latter membrane electrode assembly 10 so that hydrogen fuel can be supplied to the membrane electrode assembly 10 through the fuel passage 215D.
可以理解的是,该第一流体通道216D允许空气或氧气等流体自一个第一通道开口2161D流向另一个第一通道开口2161D,因此,该第一流体通道216D在相该膜电极组10提供反应活性物质的同时,还具有冷却作用。优选地,该第一流体通道216D的长度大于该第二流体通道217D的长度,和该第一流体通道216D的宽度小于该第二流体通道217D的宽度。It can be understood that the first fluid passage 216D allows a fluid such as air or oxygen to flow from one first passage opening 2161D to the other first passage opening 2161D. Therefore, the first fluid passage 216D provides a reaction in the phase of the membrane electrode assembly 10. At the same time as the active material, it also has a cooling effect. Preferably, the length of the first fluid passage 216D is greater than the length of the second fluid passage 217D, and the width of the first fluid passage 216D is smaller than the width of the second fluid passage 217D.
如附图之图9A所示,该流场板组20D包括至少两个流场板21D,其中该燃料电池 堆的燃料电池单元的每个膜电极组10被设置在该流场板组20D的相邻两个流场板21D之间,其中相邻两个流场板21D的前一个流场板21D的该第二流体通道217D和后一个流场板21D的该燃料通道215D被分别设置朝向该膜电极组10,从而使得反应活性物质,如空气,和燃料,如氢气,能够分别通过该第二流体通道217D和该燃料通道215D被提供给该膜电极组10。As shown in FIG. 9A of the accompanying drawings, the flow field plate group 20D includes at least two flow field plates 21D, wherein the fuel cell Each membrane electrode group 10 of the fuel cell unit of the stack is disposed between two adjacent flow field plates 21D of the flow field plate group 20D, wherein the previous flow field plate 21D of the adjacent two flow field plates 21D The second fluid passage 217D and the fuel passage 215D of the latter flow field plate 21D are respectively disposed toward the membrane electrode assembly 10 such that a reactive substance such as air, and a fuel such as hydrogen can pass through the second fluid, respectively. A channel 217D and the fuel channel 215D are supplied to the membrane electrode assembly 10.
如附图之图9A至图9F所示,该流场板组20D的每个流场板21D进一步包括一个支撑板214D,其中该支撑板214D被设置在该第一引导墙212D,其中该支撑板214D形成一个容纳槽2140D,且当该支撑板214D被设置在该第一引导墙212D时,该流场板21D的该第二引导墙213D被容纳在该支撑板214D的该容纳槽2140D中。换句话说,该流场板21D的该第二引导墙213D的高度不大于该支撑板214D的该容纳槽2140D的深度,从而使得该流场板21D的该第二引导墙213D被容纳在该支撑板214D的该容纳槽2140D内。优选地,该流场板组20D的该流场板21D的该第一引导墙212D的长度大于该第二引导墙213D的长度,从而使得该支撑板214D能够被设置在该第一引导墙212D。更优选地,该第二引导墙213D自该第一引导墙212D的中间部分延伸,从而使该支撑板214D的两个第一横向边缘2142D均能被设置在该第一引导墙212D的顶端。最优选地,该支撑板214D被可拆卸地设置在该第一引导墙212D。As shown in FIGS. 9A to 9F of the drawings, each flow field plate 21D of the flow field plate group 20D further includes a support plate 214D, wherein the support plate 214D is disposed at the first guide wall 212D, wherein the support The plate 214D forms a receiving groove 2140D, and when the supporting plate 214D is disposed at the first guiding wall 212D, the second guiding wall 213D of the flow field plate 21D is accommodated in the receiving groove 2140D of the supporting plate 214D. . In other words, the height of the second guiding wall 213D of the flow field plate 21D is not greater than the depth of the receiving groove 2140D of the supporting plate 214D, so that the second guiding wall 213D of the flow field plate 21D is accommodated therein. The receiving groove 214D is received in the receiving groove 2140D. Preferably, the length of the first guiding wall 212D of the flow field plate 21D of the flow field plate group 20D is greater than the length of the second guiding wall 213D, so that the supporting plate 214D can be disposed at the first guiding wall 212D. . More preferably, the second guiding wall 213D extends from the middle portion of the first guiding wall 212D such that both first lateral edges 2142D of the supporting plate 214D can be disposed at the top end of the first guiding wall 212D. Most preferably, the support plate 214D is detachably disposed on the first guide wall 212D.
值得注意的是,依本发明较佳实施例的该燃料电池堆的该流场板组20D的该可选实施的该支撑板214D在本发明燃料电池堆中起到装配支撑作用。换句话说,该流场板组20D的该流场板21D的该支撑板214D可不涉及对膜电极组10提供反应活性物质或燃料。因此,该流场板组20D的该流场板21D的该支撑板214D可由不导电的刚性材料制成。也就是说,该流场板组20D的该流场板21D的该支撑板214D可由具有高强度和低重量材料制成,以降低该燃料电池堆的重量功率比。It is noted that the alternately implemented support plate 214D of the flow field plate set 20D of the fuel cell stack in accordance with a preferred embodiment of the present invention functions as an assembly support in the fuel cell stack of the present invention. In other words, the support plate 214D of the flow field plate 21D of the flow field plate set 20D may not involve providing the membrane electrode assembly 10 with a reactive substance or fuel. Therefore, the support plate 214D of the flow field plate 21D of the flow field plate group 20D can be made of a non-conductive rigid material. That is, the support plate 214D of the flow field plate 21D of the flow field plate group 20D can be made of a material having high strength and low weight to reduce the weight-to-power ratio of the fuel cell stack.
如附图之图9A至图9F所示,该流场板组20D的该流场板21D的该支撑板214D具有一个外侧和一个内侧,其中该支撑板214D的该外侧被设置朝向该膜电极组10并形成一个连续密封平面210D,该流场板组20D的该流场板21D的该流场板体211D的该阳极侧2112D形成一个连续密封平面21120D,其中该流场板体211D的该阳极侧2112D的该连续密封平面21120D被设置围绕该燃料通道215D,从而使得当该燃料电池堆被堆叠时,该流场板21D的该支撑板214D的该外侧和该阳极侧2112D能够分别为该膜电极组10提供一个平的支撑,和使该支撑板214D的该外侧和该流场板体211D的该阳极侧2112D能够分别密封地抵压在该膜电极组10。 As shown in FIGS. 9A to 9F of the accompanying drawings, the support plate 214D of the flow field plate 21D of the flow field plate group 20D has an outer side and an inner side, wherein the outer side of the support plate 214D is disposed toward the film electrode. Group 10 and forming a continuous sealing plane 210D, the anode side 2112D of the flow field plate 211D of the flow field plate 21D forming a continuous sealing plane 21120D, wherein the flow field plate 211D The continuous sealing plane 21120D of the anode side 2112D is disposed around the fuel passage 215D such that when the fuel cell stack is stacked, the outer side of the support plate 214D of the flow field plate 21D and the anode side 2112D can respectively The membrane electrode assembly 10 provides a flat support, and the outer side of the support plate 214D and the anode side 2112D of the flow field plate 211D can be sealingly pressed against the membrane electrode assembly 10, respectively.
如附图之图9A至图9F所示,该流场板组20D的该流场板21D的该支撑板214D包括两个相反的端部,两个第一端部2141D和两个分别延伸在该第一端部2141D之间的第一横向边缘2142D,其中该支撑板214D的该第一端部2141D和该第一横向边缘2142D形成该容纳槽2140D和该连续密封平面210D;该流场板21D的该流场板体211D包括两个相反的端部,两个第二端部2113D、两个分别延伸在该第二端部2113D之间的第二横向边缘2114D和一个纵向地延伸在该第二横向边缘2114D之间的形成部2115D,其中该形成部2115D形成延伸在该第二端部2113D之间的燃料通道215D,其中该流场板体211D的该第二端部2113D和该第二横向边缘2114D在该流场板21D的该阳极侧2112D形成该连续密封平面21120D,其中该连续密封平面21120D被设置环绕该阳极板体212D的该形成部2115D,从而使得当该燃料电池堆被堆叠时,该流场板21D的该支撑板214D的该外侧和该阳极侧2112D能够分别为该膜电极组10提供一个平的支撑,和使该支撑板214D的该外侧和该阳极侧2112D能够分别密封地抵压在该膜电极组10。As shown in FIGS. 9A to 9F of the accompanying drawings, the support plate 214D of the flow field plate 21D of the flow field plate group 20D includes two opposite ends, and the two first end portions 2141D and the two extend respectively. a first lateral edge 2142D between the first end portions 2141D, wherein the first end portion 2141D of the support plate 214D and the first lateral edge 2142D form the receiving groove 2140D and the continuous sealing plane 210D; the flow field plate The flow field plate 211D of 21D includes two opposite ends, two second ends 2113D, two second lateral edges 2114D extending between the second ends 2113D and a longitudinal extension a forming portion 2115D between the second lateral edges 2114D, wherein the forming portion 2115D forms a fuel passage 215D extending between the second end portions 2113D, wherein the second end portion 2113D of the flow field plate body 211D and the first portion The second lateral edge 2114D forms the continuous sealing plane 21120D on the anode side 2112D of the flow field plate 21D, wherein the continuous sealing plane 21120D is disposed around the forming portion 2115D of the anode plate body 212D, such that when the fuel cell stack is The support plate 2 of the flow field plate 21D when stacked The outer side of the 14D and the anode side 2112D are capable of providing a flat support for the membrane electrode assembly 10, respectively, and enabling the outer side of the support plate 214D and the anode side 2112D to be sealingly pressed against the membrane electrode assembly 10, respectively.
可以理解的是,该流场板21D的该第一流体通道216D与该第二流体通道217D相连通以形成一个完全穿透型通道(或槽)的这种结构可使该第一流体通道216D实现本发明燃料电池堆的散热功能的同时,起到将外部反应活性流体引导至该第二流体通道217D的作用。进一步地,该流场板21D的该第一流体通道216D实现供气和散热的双重功能,且该支撑板214D的该第一端部2141D和该第一横向边缘2142D与该膜电极组10具有一个更大的接触面,从而使得当该支撑板214D为良好导热材料制成时,本发明燃料电池堆具有更好的散热效果和降低风扇转速敏感度。相应地,随着散热效应的提升和风扇转速敏感度的降低,在相同功率输出下,相对于现有技术需要构建的更大型的燃料电池,该燃料电池的整体体积和重量均能够被降低。It can be understood that the first fluid passage 216D of the flow field plate 21D communicates with the second fluid passage 217D to form a completely penetrating passage (or groove). The first fluid passage 216D can be made. While the heat dissipation function of the fuel cell stack of the present invention is achieved, the external reactive fluid is guided to the second fluid passage 217D. Further, the first fluid channel 216D of the flow field plate 21D achieves the dual functions of air supply and heat dissipation, and the first end portion 2141D and the first lateral edge 2142D of the support plate 214D and the membrane electrode assembly 10 have A larger contact surface, such that when the support plate 214D is made of a good thermally conductive material, the fuel cell stack of the present invention has better heat dissipation and reduced fan speed sensitivity. Accordingly, as the heat dissipation effect increases and the fan speed sensitivity decreases, the overall volume and weight of the fuel cell can be reduced at the same power output relative to the larger fuel cells that need to be constructed in the prior art.
如附图之图9A至图9F所示,该流场板组20D的该流场板21D的该支撑板214D包括两个第一端部2141D,和该流场板21D的该流场板体211D包括两个相反的端部,两个第二端部2113D,其中该流场板组20D的该流场板21D的支撑板214D的每个第一端部2141D具有一个第一连通开口21410D,该流场板体211D的每个第二端部2113D具有一个第二连通开口21130D,其中该支撑板214D的该第一端部2141D的该第一连通开口21410D分别与相对应的该流场板体211D的该第二端部2113D的该第二连通开口21130D相连通和形成一个燃料流道200D,其中该流场板21D的每个燃料通道215D的两端分别与该燃料流道200D相连通,从而使得氢燃料可通过该燃料电池堆的该流场板组20D的该流场板21D的该燃料流道200D被提供给该膜电极组10。 As shown in FIGS. 9A to 9F of the accompanying drawings, the support plate 214D of the flow field plate 21D of the flow field plate group 20D includes two first end portions 2141D, and the flow field plate body of the flow field plate 21D. 211D includes two opposite ends, two second ends 2113D, wherein each first end 2141D of the support plate 214D of the flow field plate 21D of the flow field plate group 20D has a first communication opening 21410D, Each of the second end portions 2113D of the flow field plate 211D has a second communication opening 21130D, wherein the first communication opening 21410D of the first end portion 2141D of the support plate 214D and the corresponding flow field plate respectively The second communication opening 21130D of the second end portion 2113D of the body 211D communicates with and forms a fuel flow path 200D, wherein both ends of each fuel passage 215D of the flow field plate 21D are respectively connected to the fuel flow path 200D. Thereby, hydrogen fuel can be supplied to the membrane electrode assembly 10 through the fuel flow path 200D of the flow field plate 21D of the flow field plate group 20D of the fuel cell stack.
如附图之图9A至图9F所示,该流场板组20D的相邻两个流场板21D之间的密封可通过一个密封垫22D而被实现,其中该密封垫22D为一空心结构,且该密封垫22D的密封部分被设置在前一个流场板21D的该流场板体211D的该阳极侧2112D的一个周缘。换言之,该密封垫22D为一中空结构以实现流体,如气体,从中通过。该密封垫22D进一步被设置与该流场板体211D的该阳极侧2112D相匹配的尺寸和形状。如图9A至图9F所示,该密封垫22D为一空心结构,且该密封垫22D的密封部分被设置在两个相邻流场板21D中的前一个流场板21D的该流场板体211D的该阳极侧2112D和后一个流场板21D的该支撑板214D之间,其中该膜电极组10的一个周缘被设置在该密封垫22D的密封部分与前一个流场板21D的该流场板体211D的该阳极侧2112D之间,从而使得前一个流场板21D的该流场板体211D、后一个流场板21D的该支撑板214D和该膜电极组10形成一个密封空间,以用于燃料流动。进一步地,该密封垫22D的两端被分别设置在前一个流场板21D的该流场板体211D的该端部和相应的后一个流场板21D的该支撑板214D的该端部之间,其中该密封垫22D被设置分别围绕前一个流场板21D的该流场板体211D的两个该第二连通开口21130D和后一个流场板21D的该支撑板214D的两个该第一连通开口21410D,从而使得当该燃料电池被组装和该密封垫22D被挤压在两个相邻流场板21D之间时,前一个流场板21D的该流场板体211D和后一个流场板21D的该支撑板214D被密封地相互堆叠在一起,以防止燃料自前一个流场板21D的该流场板体211D和后一个流场板21D的该流场板体211D之间的空隙泄漏。可以理解的是,该燃料通道215D不被该密封垫22D遮盖。优选地,该密封垫22D进一步被设置在该支撑板214D的两个端部和围绕该流场板体211D的该燃料通道215D,以形成一个密封空间用于氢流动。换句话说,该燃料通道215D不被该密封垫22D遮盖。As shown in FIGS. 9A to 9F of the accompanying drawings, the seal between the adjacent two flow field plates 21D of the flow field plate group 20D can be realized by a gasket 22D which is a hollow structure. And the sealing portion of the gasket 22D is disposed on one circumference of the anode side 2112D of the flow field plate 211D of the previous flow field plate 21D. In other words, the gasket 22D is a hollow structure to allow a fluid, such as a gas, to pass therethrough. The gasket 22D is further provided in a size and shape that matches the anode side 2112D of the flow field plate 211D. As shown in FIGS. 9A to 9F, the gasket 22D is a hollow structure, and the sealing portion of the gasket 22D is disposed in the flow field plate of the previous flow field plate 21D of the two adjacent flow field plates 21D. Between the anode side 2112D of the body 211D and the support plate 214D of the latter flow field plate 21D, wherein a circumference of the membrane electrode assembly 10 is disposed at the sealing portion of the gasket 22D and the previous flow field plate 21D The anode side 2112D of the flow field plate 211D is such that the flow field plate 211D of the previous flow field plate 21D, the support plate 214D of the latter flow field plate 21D, and the membrane electrode assembly 10 form a sealed space. For fuel flow. Further, both ends of the gasket 22D are respectively disposed at the end of the flow field plate 211D of the previous flow field plate 21D and the end portion of the support plate 214D of the corresponding subsequent flow field plate 21D. And wherein the gasket 22D is disposed to surround the two of the second communication opening 21130D of the flow field plate 211D of the previous flow field plate 21D and the two support plates 214D of the subsequent flow field plate 21D, respectively. A communication opening 21410D such that when the fuel cell is assembled and the gasket 22D is squeezed between two adjacent flow field plates 21D, the flow field plate 211D and the latter of the previous flow field plate 21D The support plates 214D of the flow field plate 21D are sealedly stacked on each other to prevent fuel from being between the flow field plate 211D of the previous flow field plate 21D and the flow field plate 211D of the latter flow field plate 21D. The gap leaks. It will be appreciated that the fuel passage 215D is not covered by the gasket 22D. Preferably, the gasket 22D is further disposed at both ends of the support plate 214D and the fuel passage 215D surrounding the flow field plate 211D to form a sealed space for hydrogen flow. In other words, the fuel passage 215D is not covered by the gasket 22D.
如附图之图9B所示,该流场板组20D的该流场板21D的该支撑板214D的该第一端部2141D被分别地和密封地设置在该流场板体211D的该第二端部2113D,以防止氢燃料通过该流场板组20D的该流场板21D的该支撑板214D的该第一端部2141D和相应的该流场板体211D的该第二端部2113D之间的空隙泄漏。因此,该流场板组20D的该流场板21D的该支撑板214D的该第一端部2141D和相应的该流场板体211D的该第二端部2113D被密封地相互耦接在一起,以防止该支撑板214D的该第一端部2141D和相应的该流场板体211D的该第二端部2113D形成位于两者之间的与该燃料流道200D相连通的空隙的形成。As shown in FIG. 9B of the drawing, the first end portion 2141D of the support plate 214D of the flow field plate 21D of the flow field plate group 20D is separately and sealingly disposed on the flow field plate body 211D. a second end portion 2113D for preventing hydrogen fuel from passing through the first end portion 2141D of the support plate 214D of the flow field plate 21D of the flow field plate group 20D and the corresponding second end portion 2113D of the flow field plate body 211D The gap between the leaks. Therefore, the first end portion 2141D of the support plate 214D of the flow field plate 21D of the flow field plate group 20D and the corresponding second end portion 2113D of the flow field plate body 211D are sealingly coupled to each other. The first end portion 2141D of the support plate 214D and the corresponding second end portion 2113D of the flow field plate body 211D are formed to form a gap between the two communicating with the fuel flow path 200D.
值得注意的是,该流场板21D的该支撑板214D的该第一端部2141D和相应的该流 场板体211D的该第二端部2113D之间的密封可通过一个被设置围绕该支撑板214D的该第一端部2141D的该第一连通开口21410D(或围绕相应的该流场板体211D的该第二端部2113D的该第二连通开口21130D)的密封环或密封圈23D而被实现。在另一些实施例中,该流场板21D的该支撑板214D的该第一端部2141D和相应的该流场板体211D的该第二端部2113D之间的密封通过将该支撑板214D的该第一端部2141D和相应的该流场板体211D的该第二端部2113D紧密贴合在一起而被实现。在其它实施例中,该支撑板214D的该第一端部2141D和相应的该流场板体211D的该第二端部2113D之间的密封通过使用胶水或粘附剂将该支撑板214D的该第一端部2141D和相应的该流场板体211D的该第二端部2113D粘附在一起而被实现。It should be noted that the first end portion 2141D of the support plate 214D of the flow field plate 21D and the corresponding flow The seal between the second end portion 2113D of the field plate body 211D may pass through the first communication opening 21410D disposed around the first end portion 2141D of the support plate 214D (or around the corresponding flow field plate body 211D) The seal ring or seal ring 23D of the second communication opening 21130D) of the second end portion 2113D is realized. In other embodiments, the seal between the first end 2141D of the support plate 214D of the flow field plate 21D and the second end portion 2113D of the corresponding flow field plate 211D passes the support plate 214D. The first end portion 2141D and the corresponding second end portion 2113D of the flow field plate body 211D are closely attached to each other. In other embodiments, the seal between the first end 2141D of the support plate 214D and the corresponding second end portion 2113D of the flow field plate 211D is achieved by using glue or adhesive to the support plate 214D. The first end portion 2141D and the corresponding second end portion 2113D of the flow field plate body 211D are adhered together to be realized.
可以理解的是,依本发明较佳实施例的该燃料电池的该阳极流场板(阳极板体或流场板体)和该阴极流场板(阴极板体或流场板体)所用的材料一般为导电金属。该金属的具有坚固、轻便且导电的特性,但该材料并不局限于金属。含有石墨、碳黑、碳纤维和/或纳米碳等的导电性复合材料,或甚至得到强化的导电石墨、碳黑、碳纤维和/或纳米碳等材料,均可用于本发明结构。It can be understood that the anode flow field plate (anode plate body or flow field plate body) and the cathode flow field plate (cathode plate body or flow field plate body) of the fuel cell according to the preferred embodiment of the present invention are used. The material is typically a conductive metal. The metal is strong, lightweight and electrically conductive, but the material is not limited to metal. Conductive composite materials containing graphite, carbon black, carbon fibers, and/or nanocarbons, or even materials such as conductive graphite, carbon black, carbon fibers, and/or nanocarbon, which are reinforced, can be used in the structure of the present invention.
本领域技术人员应理解的是,在本发明的揭露中,术语“纵向”、“横向”、“上”、“下”、“前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、“底”“内”、“外”等指示的方位或位置关系是基于附图所示的方位或位置关系,其仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此上述术语不能理解为对本发明的限制。It should be understood by those skilled in the art that in the disclosure of the present invention, the terms "longitudinal", "transverse", "upper", "lower", "front", "back", "left", "right", " The orientation or positional relationship of the indications of "upright", "horizontal", "top", "bottom", "inside", "outside", etc. is based on the orientation or positional relationship shown in the drawings, which is merely for convenience of description of the present invention and The above description of the invention is not to be construed as a limitation of the invention.
可以理解的是,术语“一”应理解为“至少一”或“一个或多个”,即在一个实施例中,一个元件的数量可以为一个,而在另外的实施例中,该元件的数量可以为多个,术语“一”不应被理解为对数量的限制。It will be understood that the term "a" is understood to mean "at least one" or "one or more", that is, in one embodiment, the number of one element may be one, and in other embodiments, the element The number may be plural, and the term "a" should not be construed as limiting the quantity.
本领域技术人员会明白附图中所示的和以上所描述的本发明实施例仅是对本发明的示例而不是限制。Those skilled in the art will appreciate that the embodiments of the invention, which are illustrated in the drawings and described above, are merely illustrative and not limiting.
由此可以看到本发明目的可被充分有效完成。用于解释本发明功能和结构原理的该实施例已被充分说明和描述,且本发明不受基于这些实施例原理基础上的改变的限制。因此,本发明包括涵盖在附属权利要求书要求范围和精神之内的所有修改。 It can thus be seen that the object of the invention can be fully and efficiently accomplished. The embodiment has been described and described in detail to explain the principles of the present invention and the invention is not to be construed as limited. Accordingly, the present invention includes all modifications that come within the scope and spirit of the appended claims.

Claims (64)

  1. 一种用于燃料电池的阴极流场板,其中该燃料电池具有一个膜电极组,其特征在于,包括一个阴极流场板,其中所述阴极流场板被布置以密封该膜电极组,其中所述阴极流场板具有一组流体通道和一组冷却通道,其中所述冷却通道分别与所述流体通道相对其和相连通。A cathode flow field plate for a fuel cell, wherein the fuel cell has a membrane electrode assembly including a cathode flow field plate, wherein the cathode flow field plate is arranged to seal the membrane electrode assembly, wherein The cathode flow field plate has a set of fluid passages and a set of cooling passages, wherein the cooling passages are in communication with the fluid passages, respectively.
  2. 根据权利要求1所述的阴极流场板,其中所述阴极流场板具有一个平面侧和一个通道侧,其中所述平面侧位于所述阴极流场板的一个内侧,其中所述通道侧位于所述阴极流场板的一个外侧,其中所述阴极流场板的所述内侧朝向该膜电极组,其中所述流体通道和所述冷却通道被形成于所述阴极流场板的所述通道侧。The cathode flow field plate of claim 1 wherein said cathode flow field plate has a planar side and a channel side, wherein said planar side is located on an inner side of said cathode flow field plate, wherein said channel side is located An outer side of the cathode flow field plate, wherein the inner side of the cathode flow field plate faces the membrane electrode set, wherein the fluid channel and the cooling channel are formed in the channel of the cathode flow field plate side.
  3. 根据权利要求2所述的阴极流场板,其中每个所述流体通道是一个从所述阴极流场板的所述外侧延伸至所述阴极流场板的所述内侧的一个穿透型通道,以使流体能够沿所述流体通道流向该膜电极组,从而促进电化学反应穿过该膜电极组发生和产生电能。The cathode flow field plate according to claim 2, wherein each of said fluid passages is a penetrating passage extending from said outer side of said cathode flow field plate to said inner side of said cathode flow field plate To enable fluid to flow along the fluid channel to the membrane electrode set, thereby facilitating electrochemical reactions to occur and generate electrical energy through the membrane electrode assembly.
  4. 根据权利要求2所述的阴极流场板,其中所述阴极流场板包括一组从所述阴极流场板的所述外侧相隔开地延伸的引导墙,以在所述引导墙之间形成所述流体通道和所述冷却通道。The cathode flow field plate according to claim 2, wherein said cathode flow field plate comprises a plurality of guide walls spaced apart from said outer side of said cathode flow field plate to be between said guide walls The fluid passage and the cooling passage are formed.
  5. 根据权利要求3所述的阴极流场板,其中所述阴极流场板包括一组从所述阴极流场板的所述外侧相隔开地延伸的引导墙,以在所述引导墙之间形成所述流体通道和所述冷却通道。The cathode flow field plate according to claim 3, wherein said cathode flow field plate comprises a plurality of guide walls spaced apart from said outer side of said cathode flow field plate to be between said guide walls The fluid passage and the cooling passage are formed.
  6. 一种用于燃料电池的阳极流场板,其中该燃料电池具有一个膜电极组,其特征在于,包括一个阳极流场板,其中所述阳极流场板具有一个平面侧和一个通道侧,其中所述平面侧位于所述阳极流场板的一个内侧,其中所述通道侧位于所述阳极流场板的一个外侧,其中所述阳极流场板的所述通道侧被设置适用于密封该膜电极组,其中所述阳极流场板进一步包括至少一个燃料通道,其中所述燃料通道形成于朝向该膜电极组的所述通道侧,从而使燃料能够通过所述燃料通道被提供给该膜电极组。An anode flow field plate for a fuel cell, wherein the fuel cell has a membrane electrode assembly including an anode flow field plate, wherein the anode flow field plate has a planar side and a channel side, wherein The planar side is located on an inner side of the anode flow field plate, wherein the channel side is located on an outer side of the anode flow field plate, wherein the channel side of the anode flow field plate is configured to seal the film An electrode group, wherein the anode flow field plate further includes at least one fuel passage, wherein the fuel passage is formed toward the passage side of the membrane electrode group, thereby enabling fuel to be supplied to the membrane electrode through the fuel passage group.
  7. 根据权利要求6所述的阳极流场板,其中所述阳极流场板进一步具有两个开口,其中所述开口被分别形成于所述阳极流场板的两个相反的端部,其中所述燃料通道的两端被分别延伸至所述开口,以引导燃料经所述燃料通道在所述开口之间流动。The anode flow field plate according to claim 6, wherein said anode flow field plate further has two openings, wherein said openings are respectively formed at opposite ends of said anode flow field plate, wherein said Both ends of the fuel passage are respectively extended to the opening to guide fuel flow between the openings through the fuel passage.
  8. 根据权利要求6所述的阳极流场板,其中每个所述燃料通道具有一个蛇形结构和凹陷在所述阳极流场板的所述通道侧。 The anode flow field plate according to claim 6, wherein each of said fuel passages has a serpentine structure and is recessed on said passage side of said anode flow field plate.
  9. 根据权利要求7所述的阳极流场板,其中每个所述燃料通道具有一个蛇形结构和凹陷在所述阳极流场板的所述通道侧。The anode flow field plate according to claim 7, wherein each of said fuel passages has a serpentine structure and is recessed on said passage side of said anode flow field plate.
  10. 根据权利要求9所述的阳极流场板,其中所述开口为穿过所述阳极流场板的所述内侧和所述外侧的穿透型槽。The anode flow field plate according to claim 9, wherein the opening is a penetrating groove that passes through the inner side and the outer side of the anode flow field plate.
  11. 一种燃料电池,其特征在于,包括:A fuel cell, comprising:
    一膜电极组;和a membrane electrode set; and
    一流场板组,其中所述流场板组包括一个阴极流场板和一个阳极流场板,其中所述膜电极组被密封于所述阴极流场板和所述阳极流场板之间;a first-rate field plate group, wherein the flow field plate group includes a cathode flow field plate and an anode flow field plate, wherein the membrane electrode assembly is sealed between the cathode flow field plate and the anode flow field plate ;
    其中所述阴极流场板具有一平面侧、一相反的通道侧和一组形成在所述通道侧的流体通道,其中所述平面侧位于所述阴极流场板的一朝向膜电极组的外侧,其中所述流体通道被设置用于使流体能够沿所述流体通道流向所述膜电极组,从而促进电化学反应穿过所述膜电极发生和产生电能;Wherein the cathode flow field plate has a planar side, an opposite channel side and a plurality of fluid channels formed on the channel side, wherein the planar side is located on a side of the cathode flow field plate facing the membrane electrode group Wherein the fluid passage is configured to enable fluid to flow along the fluid passageway to the membrane electrode set to facilitate electrochemical reaction to occur and generate electrical energy through the membrane electrode;
    其中所述阳极流场板具有一个平面侧、一个相反的通道侧和至少一个燃料通道,其中所述阳极流场板的所述平面侧位于所述阳极流场板的一个内侧,所述阳极流场板的所述通道侧位于所述阳极流场板的一个外侧和密封所述膜电极组,其中所述阳极流场板的每个所述燃料通道形成在所述阳极流场板的所述通道侧,其中所述燃料通道被设置用于使燃料能够通过所述燃料通道被提供给所述膜电极组。Wherein the anode flow field plate has a planar side, an opposite channel side and at least one fuel passage, wherein the planar side of the anode flow field plate is located on an inner side of the anode flow field plate, the anode flow The channel side of the field plate is located on an outer side of the anode flow field plate and seals the membrane electrode set, wherein each of the fuel flow channels of the anode flow field plate is formed in the anode flow field plate a channel side, wherein the fuel passage is configured to enable fuel to be supplied to the membrane electrode set through the fuel passage.
  12. 根据权利要求11所述的燃料电池,其中所述阳极流场板进一步包括两个开口,其中所述开口分别形成在所述阳极流场板的两个相反的端部,其中所述开口为穿过所述阳极流场板的所述内侧和所述外侧的穿透型槽,其中所述燃料通道的两端被分别延伸至所述开口,以引导燃料经所述燃料通道在所述开口之间流动。The fuel cell according to claim 11, wherein said anode flow field plate further comprises two openings, wherein said openings are respectively formed at opposite ends of said anode flow field plate, wherein said opening is worn Passing through the inner side and the outer penetrating groove of the anode flow field plate, wherein both ends of the fuel passage are respectively extended to the opening to guide fuel through the fuel passage at the opening Flow between.
  13. 根据权利要求12所述的燃料电池,其中每个所述燃料通道具有一个蛇形结构和凹陷在所述阳极流场板的所述通道侧。A fuel cell according to claim 12, wherein each of said fuel passages has a serpentine structure and is recessed on said passage side of said anode flow field plate.
  14. 根据权利要求13所述的燃料电池,进一步包括一个被设置在所述膜电极组和所述阳极流场板之间的密封垫,其中所述阳极流场板进一步包括一个延伸在所述端部之间的阳极板体,其中所述阳极流场板的所述阳极板体和所述端部在所述阳极流场板的所述通道侧形成一个连续密封平面,其中所述密封垫被设置在所述阳极流场板的所述密封平面。A fuel cell according to claim 13 further comprising a gasket disposed between said membrane electrode assembly and said anode flow field plate, wherein said anode flow field plate further comprises an extension at said end An anode plate body between the anode plate body and the end portion of the anode flow field plate forming a continuous sealing plane on the channel side of the anode flow field plate, wherein the gasket is set The sealing plane of the anode flow field plate.
  15. 根据权利要求14所述的燃料电池,其中当两个或更多个所述燃料电池被堆叠在一个适当位置时,前一个燃料电池被堆叠在下一个燃料电池,和前一个燃料电池的所述阳极流场板的所述平面侧与下一个燃料电池的所述阴极流场板的所述通道侧相耦接,其中 前一个燃料电池的所述阳极流场板的所述平面侧和下一个燃料电池的所述阴极流场板的所述通道侧形成两个位于两者之间的流体流道,其中所述流体流道分别与所述燃料通道相连通,以使燃料能够通过所述燃料通道从一个流体流道流向另一个流体流道。The fuel cell according to claim 14, wherein when two or more of said fuel cells are stacked in an appropriate position, a preceding fuel cell is stacked on a next fuel cell, and said anode of said previous fuel cell The planar side of the flow field plate is coupled to the channel side of the cathode flow field plate of the next fuel cell, wherein The planar side of the anode flow field plate of the previous fuel cell and the channel side of the cathode flow field plate of the next fuel cell form two fluid flow paths therebetween, wherein the fluid Flow passages are respectively in communication with the fuel passage to enable fuel to flow from one fluid flow passage to the other fluid flow passage through the fuel passage.
  16. 根据权利要求15所述的燃料电池,其中每个所述流体流道具有两个开口,其中所述密封垫被设置于所述阳极流场板的所述通道侧,以围绕所述流体流道的所述开口,以防止燃料从所述膜电极组与所述阳极流场板的所述通道侧之间的间隙泄露。A fuel cell according to claim 15, wherein each of said fluid flow paths has two openings, wherein said gasket is disposed on said channel side of said anode flow field plate to surround said fluid flow path The opening prevents leakage of fuel from a gap between the membrane electrode set and the channel side of the anode flow field plate.
  17. 根据权利要求16所述的燃料电池,其中每个所述流体流道被形成在所述阴极流场板的所述通道侧,其中一个密封槽被设置围绕所述流体流道,其中所述流场板组进一步包括两个分别被设置在所述密封槽内的密封环,以防止燃料从所述阳极流场板的所述平面侧和所述阴极流场板的所述通道侧之间的间隙泄露。A fuel cell according to claim 16, wherein each of said fluid flow paths is formed on said passage side of said cathode flow field plate, wherein a seal groove is provided around said fluid flow path, wherein said flow The field plate group further includes two seal rings respectively disposed in the seal groove to prevent fuel from between the planar side of the anode flow field plate and the channel side of the cathode flow field plate The gap leaks.
  18. 根据权利要求11所述的燃料电池,其中所述阴极流场板进一步包括一组冷却通道,其中所述冷却通道分别形成在所述阴极流场板的所述通道侧。The fuel cell according to claim 11, wherein said cathode flow field plate further comprises a plurality of cooling passages, wherein said cooling passages are respectively formed on said passage side of said cathode flow field plate.
  19. 根据权利要求18所述的燃料电池,其中所述冷却通道是均匀地形成在所述阴极流场板的穿透型通道,以分别与所述流体通道相对齐。The fuel cell according to claim 18, wherein said cooling passages are penetrating passages uniformly formed in said cathode flow field plates to be aligned with said fluid passages, respectively.
  20. 根据权利要求18所述的燃料电池,其中所述冷却通道与所述流体通道相交替地设置。The fuel cell according to claim 18, wherein said cooling passage is alternately disposed with said fluid passage.
  21. 一种用于燃料电池的流场板组,其中该燃料电池具有至少一个膜电极组,其特征在于,包括至少两个流场板,其中所述燃料电池的该膜电极组被分别设置在相邻两个流场板之间,其中每个流场板包括一个阴极板体、一个阳极板体和一组引导墙,其中所述阴极板体形成一组相互隔开的第一流体槽,其中所述引导墙被相隔开地设置在所述阴极板体和所述阳极板体之间,从而使得每相邻两个引导墙形成一个位于两者之间的第二流体槽,其中所述阴极板体的所述第一流体槽被设置分别与所述第二流体槽相连通,从而使得每个第一流体槽与相应的第二流体槽形成至少一个连续的流体通道,其中所述流体通道具有一个第一通道开口、一个第二通道开口和一个第三通道开口,其中所述流场板的所述阳极板体具有至少一个被设置在所述阳极板体的一个外侧的燃料通道,其中每相邻两个流场板的前一个流场板的所述阳极板体的所述外侧被设置朝向所述燃料电池的被设置在相邻两个流场板之间的该膜电极组,从而使燃料能够通过所述燃料通道被提供给该膜电极组,后一个流场板的所述阴极板体的所述流体通道的所述第三通道开口被设置朝向该膜电极组,从而使得所述流体通道允许流体流动在所述流体通道的所述第一通道开口和所述第二通道开口之间,并通过所述第三通道开口被提供给所述燃料电池的该膜电极组。 A flow field plate set for a fuel cell, wherein the fuel cell has at least one membrane electrode set, characterized in that it comprises at least two flow field plates, wherein the membrane electrode sets of the fuel cells are respectively disposed in phases Between two flow field plates, wherein each flow field plate comprises a cathode plate body, an anode plate body and a set of guiding walls, wherein the cathode plate body forms a set of first fluid grooves spaced apart from each other, wherein The guide walls are spaced apart between the cathode plate body and the anode plate body such that each adjacent two guide walls form a second fluid groove between the two, wherein The first fluid grooves of the cathode plate body are disposed to communicate with the second fluid grooves, respectively, such that each of the first fluid grooves and the corresponding second fluid groove form at least one continuous fluid passage, wherein the fluid The passage has a first passage opening, a second passage opening and a third passage opening, wherein the anode plate body of the flow field plate has at least one fuel passage disposed on an outer side of the anode plate body The outer side of the anode plate body of the previous flow field plate of each adjacent two flow field plates is disposed toward the membrane electrode of the fuel cell disposed between adjacent two flow field plates a group such that fuel can be supplied to the membrane electrode assembly through the fuel passage, and the third passage opening of the fluid passage of the cathode plate body of the latter flow field plate is disposed toward the membrane electrode assembly Thereby causing the fluid passage to allow fluid to flow between the first passage opening and the second passage opening of the fluid passage and to be supplied to the membrane electrode of the fuel cell through the third passage opening group.
  22. 根据权利要求21所述的流场板组,其中相邻两个流场板的前一个流场板的所述阳极板体的所述外侧形成一个用于密封所述燃料电池的所述膜电池组的连续密封平面,后一个流场板的所述阴极板体的一个外侧形成另一个用于密封所述燃料电池的所述膜电池组的连续密封平面,从而将该膜电极组密封在相邻两个流场板之间。The flow field plate set according to claim 21, wherein said outer side of said anode plate body of a preceding flow field plate of adjacent two flow field plates forms a film battery for sealing said fuel cell a continuous sealing plane of the group, one outer side of the cathode plate body of the latter flow field plate forming another continuous sealing plane for sealing the membrane battery of the fuel cell, thereby sealing the membrane electrode assembly in the phase Adjacent between two flow field plates.
  23. 根据权利要求21所述的流场板组,其中每个流场板的所述阴极板体具有两个被分别设置在所述阴极板体的两个端部的第一连通开口,所述阳极板体具有两个被分别设置在所述阳极板体的两个端部的第二连通开口,其中所述阴极板体的所述第一连通开口分别与相对应的所述阳极板体的所述第二连通开口相连通和形成一个燃料流道,其中所述流场板的每个燃料通道的两端分别与所述燃料流道相连通,从而使得燃料可通过所述流场板的所述燃料流道被提供给该膜电极组。The flow field plate set according to claim 21, wherein said cathode plate body of each flow field plate has two first communication openings respectively provided at both end portions of said cathode plate body, said anode The plate body has two second communication openings respectively disposed at both ends of the anode plate body, wherein the first communication openings of the cathode plate bodies respectively correspond to the corresponding anode plate bodies The second communication opening is in communication with and forms a fuel flow passage, wherein both ends of each fuel passage of the flow field plate are respectively in communication with the fuel flow passage, so that fuel can pass through the flow field plate The fuel flow path is supplied to the membrane electrode assembly.
  24. 根据权利要求23所述的流场板组,其中每个流场板的所述阴极板体的两个端部被分别地和密封地设置在所述阳极板体的两个端部,以防止燃料通过所述流场板的所述阴极板体的所述端部和相应的所述阳极板体的所述端部之间的空隙泄漏。The flow field plate set according to claim 23, wherein both end portions of said cathode plate body of each flow field plate are separately and sealingly disposed at both end portions of said anode plate body to prevent Fuel leaks through a gap between the end of the cathode plate body of the flow field plate and the end of the corresponding anode plate body.
  25. 根据权利要求21所述的流场板组,其中每个流场板的所述引导墙与所述阳极板体一体成型和自所述阳极板体的一个内侧延伸。The flow field plate set according to claim 21, wherein said guide wall of each flow field plate is integrally formed with said anode plate body and extends from an inner side of said anode plate body.
  26. 根据权利要求24所述的流场板组,其中每个流场板的所述引导墙与所述阳极板体一体成型和自所述阳极板体的所述内侧延伸。The flow field plate set according to claim 24, wherein said guide wall of each flow field plate is integrally formed with said anode plate body and extends from said inner side of said anode plate body.
  27. 根据权利要求21所述的流场板组,其中所述流场板的所述阴极板体具有一个形成在所述阴极板体的一个内侧的容纳槽,其中所述容纳槽的形状和大小依所述流场板的所述引导墙被设置,以能够将所述流场板的所述引导墙容纳于其内,并使所述引导墙形成的所述第二流体槽分别与所述阴极板体的所述第一流体槽相连通,从而形成所述流体通道。The flow field plate set according to claim 21, wherein said cathode plate body of said flow field plate has a receiving groove formed on an inner side of said cathode plate body, wherein said receiving groove has a shape and a size The guide wall of the flow field plate is disposed to be capable of accommodating the guide wall of the flow field plate therein, and the second fluid groove formed by the guide wall and the cathode, respectively The first fluid slots of the plate are in communication to form the fluid passage.
  28. 根据权利要求26所述的流场板组,其中所述流场板的所述阴极板体具有一个形成在所述阴极板体的一个内侧的容纳槽,其中所述容纳槽的形状和大小依所述流场板的所述引导墙被设置,以能够将所述流场板的所述引导墙容纳于其内,并使所述引导墙形成的所述第二流体槽分别与所述阴极板体的所述第一流体槽相连通,从而形成所述流体通道。The flow field plate set according to claim 26, wherein said cathode plate body of said flow field plate has a receiving groove formed on an inner side of said cathode plate body, wherein said receiving groove has a shape and a size The guide wall of the flow field plate is disposed to be capable of accommodating the guide wall of the flow field plate therein, and the second fluid groove formed by the guide wall and the cathode, respectively The first fluid slots of the plate are in communication to form the fluid passage.
  29. 根据权利要求23所述的流场板组,进一步包括两个密封环,其中所述密封环被分别设置在所述流场板的所述阳极板体的端部和相应的所述阴极板体的端部之间,其中每个密封环被设置分别环绕所述流场板的所述阴极板体的所述第一连通开口和所述阳极 板体的所述第二连通开口,以使所述流场板的所述阴极板体的两个端部被分别地和密封地设置在所述阳极板体的两个端部。The flow field plate set according to claim 23, further comprising two seal rings, wherein the seal rings are respectively disposed at ends of the anode plate body of the flow field plate and the corresponding cathode plate body Between the ends, wherein each seal ring is disposed around the first communication opening and the anode of the cathode plate body of the flow field plate, respectively The second communication opening of the plate body such that both end portions of the cathode plate body of the flow field plate are separately and sealingly disposed at both ends of the anode plate body.
  30. 根据权利要求28所述的流场板组,其中所述流场板的所述阴极板体的所述容纳槽的深度与所述流场板的所述引导墙的高度相同,从而使得所述流场板的所述引导墙能够被相适配地容纳在所述阴极板体的所述容纳槽。The flow field plate set according to claim 28, wherein a depth of said receiving groove of said cathode plate body of said flow field plate is the same as a height of said guide wall of said flow field plate, thereby causing said The guide wall of the flow field plate can be accommodated in the receiving groove of the cathode plate body.
  31. 一种燃料电池,其特征在于,包括:A fuel cell, comprising:
    至少一个膜电极组;和At least one membrane electrode set; and
    一个流场板组,其中所述流场板组包括至少两个流场板,其中所述膜电极组分别被设置在相邻两个流场板之间,其中每个流场板包括一个阴极板体、一个阳极板体和一组引导墙,其中所述阴极板体形成一组相互隔开的第一流体槽,其中所述引导墙被相隔开地设置在所述阴极板体和所述阳极板体之间,从而使得每相邻两个引导墙形成一个位于两者之间的第二流体槽,其中所述阴极板体的所述第一流体槽被设置分别与所述第二流体槽相连通,从而使得每个第一流体槽与相应的第二流体槽形成至少一个连续的流体通道,其中所述流体通道具有一个第一通道开口、一个第二通道开口和一个第三通道开口,其中所述流场板的所述阳极板体具有至少一个被设置在所述阳极板体的一个外侧的燃料通道,其中相邻两个流场板的前一个流场板的所述阳极板体的所述外侧被设置朝向被设置在相邻两个流场板之间的所述膜电极组,从而使燃料能够通过所述燃料通道被提供给所述膜电极组,后一个流场板的所述阴极板体的所述流体通道的所述第三通道开口被设置朝向所述膜电极组,从而使得所述流体通道允许流体流动在所述流体通道的所述第一通道开口和所述第二通道开口之间,并通过所述第三通道开口被提供给所述膜电极组。a flow field plate set, wherein the flow field plate set includes at least two flow field plates, wherein the membrane electrode sets are respectively disposed between adjacent two flow field plates, wherein each flow field plate includes a cathode a plate body, an anode plate body and a set of guide walls, wherein the cathode plate body forms a set of spaced apart first fluid grooves, wherein the guide walls are spaced apart from each other at the cathode plate body and Between the anode plates, such that each adjacent two guiding walls form a second fluid groove between the two, wherein the first fluid grooves of the cathode plate are respectively disposed with the second The fluid slots are in communication such that each of the first fluid slots and the respective second fluid slots form at least one continuous fluid passage, wherein the fluid passage has a first passage opening, a second passage opening, and a third passage An opening, wherein the anode plate body of the flow field plate has at least one fuel passage disposed on an outer side of the anode plate body, wherein the anode of a previous flow field plate of two adjacent flow field plates The outer part of the board Provided toward the membrane electrode assembly disposed between adjacent two flow field plates such that fuel can be supplied to the membrane electrode assembly through the fuel passage, the cathode plate of the latter flow field plate The third passage opening of the fluid passage of the body is disposed toward the membrane electrode assembly such that the fluid passage allows fluid to flow in the first passage opening and the second passage opening of the fluid passage Between and through the third passage opening is provided to the membrane electrode assembly.
  32. 根据权利要求31所述的燃料电池,其中相邻两个流场板的前一个流场板的所述阳极板体的所述外侧形成一个用于密封所述膜电池组的连续密封平面,后一个流场板的所述阴极板体的一个外侧形成另一个用于密封所述膜电池组的连续密封平面,从而将所述膜电极组密封在相邻两个流场板之间。A fuel cell according to claim 31, wherein said outer side of said anode plate body of a preceding flow field plate of adjacent two flow field plates forms a continuous sealing plane for sealing said film battery pack, One outer side of the cathode plate body of one flow field plate forms another continuous sealing plane for sealing the film battery pack to seal the membrane electrode assembly between adjacent two flow field plates.
  33. 根据权利要求31所述的燃料电池,其中每个流场板的所述阴极板体具有两个被分别设置在所述阴极板体的两个端部的第一连通开口,所述阳极板体具有两个被分别设置在所述阳极板体的两个端部的第二连通开口,其中所述阴极板体的所述第一连通开口分别与相对应的所述阳极板体的所述第二连通开口相连通和形成一个燃料流道,其中所述流场板的每个燃料通道的两端分别与所述燃料流道相连通,从而使得燃料可通过所述流场板的所述燃料流道被提供给所述膜电极组。 A fuel cell according to claim 31, wherein said cathode plate body of each flow field plate has two first communication openings respectively provided at both end portions of said cathode plate body, said anode plate body Having two second communication openings respectively disposed at both ends of the anode plate body, wherein the first communication openings of the cathode plate bodies respectively correspond to the corresponding portions of the anode plate body Two communication openings are in communication and forming a fuel flow passage, wherein both ends of each fuel passage of the flow field plate are respectively in communication with the fuel flow passage such that fuel can pass through the fuel of the flow field plate A flow channel is provided to the membrane electrode assembly.
  34. 根据权利要求33所述的燃料电池,其中每个流场板的所述阴极板体的两个端部被分别地和密封地设置在所述阳极板体的两个端部,以防止燃料通过所述流场板的所述阴极板体的所述端部和相应的所述阳极板体的所述端部之间的空隙泄漏。A fuel cell according to claim 33, wherein both end portions of said cathode plate body of each flow field plate are separately and sealingly disposed at both ends of said anode plate body to prevent fuel from passing through A gap between the end of the cathode plate body of the flow field plate and the end portion of the corresponding anode plate body leaks.
  35. 根据权利要求31所述的燃料电池,其中每个流场板的所述引导墙与所述阳极板体一体成型和自所述阳极板体的一个内侧延伸。A fuel cell according to claim 31, wherein said guide wall of each flow field plate is integrally formed with said anode plate body and extends from one inner side of said anode plate body.
  36. 根据权利要求34所述的燃料电池,其中每个流场板的所述引导墙与所述阳极板体一体成型和自所述阳极板体的所述内侧延伸。A fuel cell according to claim 34, wherein said guide wall of each flow field plate is integrally formed with said anode plate body and extends from said inner side of said anode plate body.
  37. 根据权利要求31所述的燃料电池,其中所述流场板的所述阴极板体具有一个形成在所述阴极板体的一个内侧的容纳槽,其中所述容纳槽的形状和大小依所述流场板的所述引导墙被设置,以能够将所述流场板的所述引导墙容纳于其内,并使所述引导墙形成的所述第二流体槽分别与所述阴极板体的所述第一流体槽相连通,从而形成所述流体通道。A fuel cell according to claim 31, wherein said cathode plate body of said flow field plate has a receiving groove formed on an inner side of said cathode plate body, wherein said receiving groove has a shape and a size according to said The guide wall of the flow field plate is disposed to be capable of accommodating the guide wall of the flow field plate therein, and the second fluid groove formed by the guide wall and the cathode plate body respectively The first fluid slots are in communication to form the fluid passage.
  38. 根据权利要求33所述的燃料电池,进一步包括两个密封环,其中所述密封环被分别设置在所述流场板的所述阳极板体的端部和相应的所述阴极板体的端部之间,其中每个密封环被设置分别环绕所述流场板的所述阴极板体的所述第一连通开口和所述阳极板体的所述第二连通开口,以使所述流场板的所述阴极板体的两个端部被分别地和密封地设置在所述阳极板体的两个端部。A fuel cell according to claim 33, further comprising two seal rings, wherein said seal rings are respectively disposed at ends of said anode plate bodies of said flow field plates and respective ends of said cathode plates Between the portions, wherein each of the seal rings is disposed to surround the first communication opening of the cathode plate body of the flow field plate and the second communication opening of the anode plate body, respectively, to make the flow Both ends of the cathode plate body of the field plate are separately and sealingly disposed at both ends of the anode plate body.
  39. 根据权利要求31所述的燃料电池,进一步包括至少一个密封垫,其中所述密封垫分别被设置在两个相邻流场板的前一个流场板的所述阳极板体的所述外侧,其中所述密封垫为一空心结构,且所述密封垫的密封部分被设置在前一个流场板的所述阳极板体和后一个流场板的所述阴极板体之间和所述膜电极组的周缘被设置在所述密封垫的密封部分与前一个流场板的所述阳极板体之间,从而使得前一个流场板的所述阳极板体、后一个流场板的所述阴极板体和所述膜电极组形成一个密封空间,以用于燃料流动。A fuel cell according to claim 31, further comprising at least one gasket, wherein said gaskets are respectively disposed on said outer side of said anode plate body of a preceding flow field plate of two adjacent flow field plates, Wherein the gasket is a hollow structure, and a sealing portion of the gasket is disposed between the anode plate body of the previous flow field plate and the cathode plate body of the latter flow field plate and the film The periphery of the electrode group is disposed between the sealing portion of the gasket and the anode plate body of the previous flow field plate, such that the anode plate body and the latter flow field plate of the previous flow field plate The cathode plate body and the membrane electrode group form a sealed space for fuel flow.
  40. 根据权利要求39所述的燃料电池,其中所述密封垫的两端被分别设置在前一个流场板的所述阳极板体的所述端部和相应的后一个流场板的所述阴极流场板的所述端部之间,其中所述密封垫被设置分别围绕前一个流场板的所述阳极板体的两个第一连通开口和后一个流场板的所述阴极流场板的两个第二连通开口,从而使得当所述燃料电池被组装和所述密封垫被挤压在两个流场板之间时,前一个流场板的所述阳极板体和后一个流场板的所述阴极板体被密封地相互堆叠在一起,以防止燃料自前一个流场板的所述阳极板体和后一个流场板的所述阴极板体之间的空隙泄漏。 A fuel cell according to claim 39, wherein both ends of said gasket are respectively disposed at said end portion of said anode plate body of said previous flow field plate and said cathode of said corresponding latter flow field plate Between the ends of the flow field plate, wherein the gasket is disposed to surround the two first communication openings of the anode plate body of the previous flow field plate and the cathode flow field of the latter flow field plate Two second communication openings of the plate such that when the fuel cell is assembled and the gasket is squeezed between the two flow field plates, the anode plate body and the latter one of the previous flow field plate The cathode plates of the flow field plates are sealedly stacked on each other to prevent leakage of fuel from the gap between the anode plate body of the previous flow field plate and the cathode plate body of the latter flow field plate.
  41. 一种用于燃料电池的流场板组,其中该燃料电池具有至少一个膜电极组,其特征在于,包括至少两个流场板,其中所述燃料电池的该膜电极组被分别设置在相邻两个流场板之间,其中每个流场板包括一个流场板体、一组第一引导墙和一组第二引导墙,其中所述流场板体具有一个阴极侧和一个阳极侧,其中所述流场板体具有至少一个被设置在所述阳极侧的燃料通道,其中所述第一引导墙被相隔开地设置在所述流场板体的所述阴极侧,所述第二引导墙分别自所述第一引导墙延伸,从而使得相邻两个第一引导墙形成一个位于两者之间的第一流体通道,和相应的相邻两个第二引导墙形成一个位于两者之间的第二流体通道,其中所述第一流体通道与所述第二流体通道相连通,其中每个第一流体通道具有两个第一通道开口,每个第二流体通道具有一个第二通道开口,其中相邻两个流场板的前一个流场板的所述流场板体的所述阳极侧被设置朝向被设置在相邻两个流场板之间的该膜电极组,从而使燃料能够通过所述燃料通道被提供给该膜电极组,和后一个流场板的所述流场板体的所述第二流体通道的所述第二通道开口被设置朝向所述燃料电池的该膜电极组,从而使得所述第一流体通道允许流体流动在所述流体通道的所述第一通道开口之间,并通过所述第二流体通道的所述第二通道开口被提供给所述燃料电池的该膜电极组。A flow field plate set for a fuel cell, wherein the fuel cell has at least one membrane electrode set, characterized in that it comprises at least two flow field plates, wherein the membrane electrode sets of the fuel cells are respectively disposed in phases Between two flow field plates, wherein each flow field plate comprises a flow field plate body, a set of first guide walls and a set of second guide walls, wherein the flow field plate body has a cathode side and an anode a side, wherein the flow field plate body has at least one fuel passage disposed on the anode side, wherein the first guide wall is spaced apart from the cathode side of the flow field plate body, The second guiding walls respectively extend from the first guiding wall such that adjacent two first guiding walls form a first fluid passage between the two, and corresponding two adjacent second guiding walls are formed a second fluid passage between the two, wherein the first fluid passage is in communication with the second fluid passage, wherein each first fluid passage has two first passage openings, each second fluid passage Has a second channel a port in which the anode side of the flow field plate of the previous flow field plate of two adjacent flow field plates is disposed toward the membrane electrode group disposed between adjacent two flow field plates, thereby Providing fuel to the membrane electrode set through the fuel passage, and the second passage opening of the second fluid passage of the flow field plate of the latter flow field plate is disposed toward the fuel cell The membrane electrode assembly such that the first fluid passage allows fluid to flow between the first passage openings of the fluid passage and is provided to the second passage opening of the second fluid passage The membrane electrode assembly of the fuel cell.
  42. 根据权利要求41所述的流场板组,其中每个所述流场板进一步包括一个支撑板,其中所述支撑板被设置在所述第一引导墙,其中相邻两个流场板的前一个流场板的所述流场板体的所述阳极侧形成一个用于密封被设置在相邻两个流场板之间的该膜电极组的连续密封平面,后一个流场板的所述支撑板的一个外侧形成另一个用于密封被设置在相邻两个流场板之间的该膜电极组的连续密封平面,以将该膜电极组密封在相邻两个流场板之间。The flow field plate set according to claim 41, wherein each of said flow field plates further comprises a support plate, wherein said support plate is disposed on said first guide wall, wherein adjacent flow field plates are The anode side of the flow field plate of the previous flow field plate forms a continuous sealing plane for sealing the membrane electrode set disposed between adjacent two flow field plates, the latter flow field plate One outer side of the support plate forms another continuous sealing plane for sealing the membrane electrode set disposed between adjacent two flow field plates to seal the membrane electrode assembly in adjacent two flow field plates between.
  43. 根据权利要求42所述的流场板组,其中所述支撑板形成一个容纳槽,且当所述支撑板被设置在所述第一引导墙时,所述流场板的所述第二引导墙被容纳在所述支撑板的所述容纳槽内。A flow field plate set according to claim 42, wherein said support plate forms a receiving groove, and said second guide of said flow field plate when said support plate is disposed at said first guide wall A wall is received in the receiving groove of the support plate.
  44. 根据权利要求42所述的流场板组,其中每个流场板的所述支撑板具有两个被分别设置在所述支撑板的两个端部的第一连通开口,所述流场板体具有两个被分别设置在所述流场板体的两个端部的第二连通开口,其中所述支撑板的所述第一连通开口分别与相对应的所述流场板体的所述第二连通开口相连通和形成一个燃料流道,其中所述流场板的每个燃料通道的两端分别与所述燃料流道相连通,从而使得燃料可通过所述流场板的所述燃料流道被提供给该膜电极组。 A flow field plate set according to claim 42, wherein said support plate of each flow field plate has two first communication openings respectively provided at both ends of said support plate, said flow field plate The body has two second communication openings respectively disposed at both ends of the flow field plate body, wherein the first communication opening of the support plate and the corresponding flow field plate body respectively The second communication opening is in communication with and forms a fuel flow passage, wherein both ends of each fuel passage of the flow field plate are respectively in communication with the fuel flow passage, so that fuel can pass through the flow field plate The fuel flow path is supplied to the membrane electrode assembly.
  45. 根据权利要求44所述的流场板组,其中每个流场板的所述支撑板的两个端部被分别地和密封地设置在所述流场板体的两个端部,以防止燃料通过所述流场板的所述支撑板的所述端部和相应的所述流场板体的所述端部之间的空隙泄漏。The flow field plate set according to claim 44, wherein both end portions of said support plate of each flow field plate are separately and sealingly disposed at both ends of said flow field plate to prevent Fuel leaks through a gap between the end of the support plate of the flow field plate and the end of the corresponding flow field plate.
  46. 根据权利要求41所述的流场板组,其中每个流场板的所述第一引导墙与所述流场板体一体成型和自所述流场板体的所述阴极侧延伸。The flow field plate set according to claim 41, wherein said first guide wall of each flow field plate is integrally formed with said flow field plate body and extends from said cathode side of said flow field plate body.
  47. 根据权利要求41所述的流场板组,其中所述流场板的所述支撑板具有一个容纳槽,其中所述容纳槽的形状和大小依所述流场板的所述第二引导墙被设置,以能够将所述流场板的所述第二引导墙容纳于其内。The flow field plate set according to claim 41, wherein said support plate of said flow field plate has a receiving groove, wherein said receiving groove has a shape and a size according to said second guiding wall of said flow field plate Provided to be able to accommodate the second guide wall of the flow field plate therein.
  48. 根据权利要求45所述的流场板组,进一步包括两个密封环,其中所述密封环被分别设置在所述流场板的所述流场板体的端部和相应的所述支撑板的端部之间,其中每个密封环被设置分别环绕所述流场板的所述支撑板的所述第一连通开口和所述流场板体的所述第二连通开口,以使所述流场板的所述支撑板的两个端部被分别地和密封地设置在所述流场板体的两个端部。A flow field plate set according to claim 45, further comprising two seal rings, wherein said seal rings are respectively disposed at ends of said flow field plates of said flow field plates and corresponding said support plates Between the ends, wherein each sealing ring is disposed to surround the first communication opening of the support plate of the flow field plate and the second communication opening of the flow field plate, respectively, to Both ends of the support plate of the flow field plate are separately and sealingly disposed at both ends of the flow field plate.
  49. 根据权利要求47所述的流场板组,其中所述流场板的所述流场板体的所述容纳槽的深度与所述流场板的所述第二引导墙的高度相同,从而使得所述流场板的所述第二引导墙能够被相适配地容纳在所述流场板体的所述容纳槽。The flow field plate set according to claim 47, wherein a depth of said receiving groove of said flow field plate of said flow field plate is the same as a height of said second guiding wall of said flow field plate, thereby The second guiding wall of the flow field plate can be adapted to be accommodated in the receiving groove of the flow field plate.
  50. 根据权利要求41所述的流场板组,其中所述流场板的所述流场板体的所述第一引导墙的长度大于所述流场板的所述第二引导墙的长度,以允许所述支撑板被设置在所述第一引导墙。The flow field plate set according to claim 41, wherein a length of the first guiding wall of the flow field plate of the flow field plate is greater than a length of the second guiding wall of the flow field plate, To allow the support plate to be disposed on the first guide wall.
  51. 根据权利要求42、43、44、45、46、47、48、49或50所述的流场板组,其中所述支撑板由不导电刚性材料制成。A flow field plate set according to claim 42, 43, 44, 45, 46, 47, 48, 49 or 50, wherein said support plate is made of a non-conductive rigid material.
  52. 一种燃料电池,其特征在于,包括:A fuel cell, comprising:
    至少一个膜电极组;和At least one membrane electrode set; and
    至少两个流场板,其中所述膜电极组被分别设置在相邻两个流场板之间,其中每个流场板包括一个流场板体、一组第一引导墙和一组第二引导墙,其中所述流场板体具有一个阴极侧和一个阳极侧,其中所述流场板体具有至少一个被设置在所述阳极侧的燃料通道,其中所述第一引导墙被相隔开地设置在所述流场板体的所述阴极侧,所述第二引导墙分别自所述第一引导墙延伸,从而使得相邻两个第一引导墙形成一个位于两者之间的第一流体通道,和相应的相邻两个第二引导墙形成一个位于两者之间的第二流体通道,其中所述第一流体通道与所述第二流体通道相连通,其中每个第一流体通道具有两个第一通道开 口,每个第二流体通道具有一个第二通道开口,其中相邻两个流场板的前一个流场板的所述流场板体的所述阳极侧被设置朝向被设置在相邻两个流场板之间的所述膜电极组,从而使燃料能够通过所述燃料通道被提供给所述膜电极组,和后一个流场板的所述流场板体的所述第二流体通道的所述第二通道开口被设置朝向所述燃料电池的所述膜电极组,从而使得所述第一流体通道允许流体流动在所述流体通道的所述第一通道开口之间,并通过所述第二流体通道的所述第二通道开口被提供给所述燃料电池的所述膜电极组。At least two flow field plates, wherein the membrane electrode sets are respectively disposed between adjacent two flow field plates, wherein each flow field plate comprises a flow field plate body, a set of first guide walls and a group of a guide wall, wherein the flow field plate has a cathode side and an anode side, wherein the flow field plate body has at least one fuel passage disposed on the anode side, wherein the first guide wall is phased Separatingly disposed on the cathode side of the flow field plate body, the second guiding walls respectively extending from the first guiding wall, such that two adjacent first guiding walls form one between the two a first fluid passage, and a corresponding adjacent two second guide walls forming a second fluid passage therebetween, wherein the first fluid passage is in communication with the second fluid passage, wherein each The first fluid passage has two first passages open Port, each of the second fluid passages has a second passage opening, wherein the anode side of the flow field plate of the previous flow field plate of the adjacent two flow field plates is disposed toward the adjacent two The membrane electrode assembly between the flow field plates such that fuel can be supplied to the membrane electrode assembly through the fuel passage, and the second fluid of the flow field plate of the latter flow field plate The second passage opening of the passage is disposed toward the membrane electrode set of the fuel cell such that the first fluid passage allows fluid to flow between the first passage openings of the fluid passage and through The second passage opening of the second fluid passage is provided to the membrane electrode set of the fuel cell.
  53. 根据权利要求52所述的燃料电池,其中每个所述流场板进一步包括一个支撑板,其中所述支撑板被设置在所述第一引导墙,其中相邻两个流场板的前一个流场板的所述流场板体的所述阳极侧形成一个用于密封被设置在相邻两个流场板之间的所述膜电极组的连续密封平面,后一个流场板的所述支撑板的一个外侧形成另一个用于密封被设置在相邻两个流场板之间的所述膜电极组的连续密封平面,以将所述膜电极组密封在相邻两个流场板之间。A fuel cell according to claim 52, wherein each of said flow field plates further comprises a support plate, wherein said support plate is disposed at said first guide wall, wherein a previous one of adjacent two flow field plates The anode side of the flow field plate of the flow field plate forms a continuous sealing plane for sealing the membrane electrode assembly disposed between adjacent two flow field plates, the latter flow field plate One outer side of the support plate forms another continuous sealing plane for sealing the membrane electrode set disposed between adjacent two flow field plates to seal the membrane electrode assembly in two adjacent flow fields Between the boards.
  54. 根据权利要求53所述的燃料电池,其中所述支撑板形成一个容纳槽,其中所述支撑板被设置在所述第一引导墙和所述流场板的所述第二引导墙被容纳在所述支撑板的所述容纳槽内。A fuel cell according to claim 53, wherein said support plate forms a receiving groove, and wherein said support plate is accommodated in said first guide wall and said second guide wall of said flow field plate are accommodated The receiving groove of the support plate.
  55. 根据权利要求53所述的燃料电池,其中每个流场板的所述支撑板具有两个被分别设置在所述支撑板的两个端部的第一连通开口,所述流场板体具有两个被分别设置在所述流场板体的两个端部的第二连通开口,其中所述支撑板的所述第一连通开口分别与相对应的所述流场板体的所述第二连通开口相连通和形成一个燃料流道,其中所述流场板的每个燃料通道的两端分别与所述燃料流道相连通,从而使得燃料可通过所述流场板的所述燃料流道被提供给所述膜电极组。A fuel cell according to claim 53, wherein said support plate of each flow field plate has two first communication openings respectively provided at both ends of said support plate, said flow field plate having Two second communication openings respectively disposed at both ends of the flow field plate, wherein the first communication openings of the support plates are respectively corresponding to the corresponding ones of the flow field plates Two communication openings are in communication and forming a fuel flow passage, wherein both ends of each fuel passage of the flow field plate are respectively in communication with the fuel flow passage such that fuel can pass through the fuel of the flow field plate A flow channel is provided to the membrane electrode assembly.
  56. 根据权利要求55所述的燃料电池,其中每个流场板的所述支撑板的两个端部被分别地和密封地设置在所述流场板体的两个端部,以防止燃料通过所述流场板的所述支撑板的所述端部和相应的所述流场板体的所述端部之间的空隙泄漏。A fuel cell according to claim 55, wherein both end portions of said support plate of each flow field plate are separately and sealingly disposed at both ends of said flow field plate to prevent fuel from passing through A gap between the end of the support plate of the flow field plate and the end of the corresponding flow field plate leaks.
  57. 根据权利要求52所述的燃料电池,其中每个流场板的所述第一引导墙与所述流场板体一体成型和自所述流场板体的所述阴极侧延伸。A fuel cell according to claim 52, wherein said first guide wall of each flow field plate is integrally formed with said flow field plate body and extends from said cathode side of said flow field plate body.
  58. 根据权利要求52所述的燃料电池,其中所述流场板的所述支撑板具有一个容纳槽,其中所述容纳槽的形状和大小依所述流场板的所述第二引导墙被设置,以能够将所述流场板的所述第二引导墙容纳于其内。A fuel cell according to claim 52, wherein said support plate of said flow field plate has a receiving groove, wherein said receiving groove is shaped and sized according to said second guiding wall of said flow field plate So that the second guiding wall of the flow field plate can be accommodated therein.
  59. 根据权利要求56所述的燃料电池,进一步包括两个密封环,其中所述密封环 被分别设置在所述流场板的所述流场板体的端部和相应的所述支撑板的端部之间,其中每个密封环被设置分别环绕所述流场板的所述支撑板的所述第一连通开口和所述流场板体的所述第二连通开口,以使所述流场板的所述支撑板的两个端部被分别地和密封地设置在所述流场板体的两个端部。A fuel cell according to claim 56, further comprising two seal rings, wherein said seal ring Separately disposed between an end of the flow field plate of the flow field plate and an end of the corresponding support plate, wherein each seal ring is disposed to surround the support of the flow field plate The first communication opening of the plate and the second communication opening of the flow field plate such that both ends of the support plate of the flow field plate are separately and sealingly disposed at the The two ends of the flow field plate.
  60. 根据权利要求58所述的燃料电池,其中所述流场板的所述流场板体的所述容纳槽的深度与所述流场板的所述第二引导墙的高度相同,从而使得所述流场板的所述第二引导墙能够被相适配地容纳在所述流场板体的所述容纳槽。A fuel cell according to claim 58, wherein a depth of said accommodating groove of said flow field plate of said flow field plate is the same as a height of said second guide wall of said flow field plate, thereby The second guide wall of the flow field plate can be adapted to be accommodated in the receiving groove of the flow field plate.
  61. 根据权利要求52所述的燃料电池,其中所述流场板的所述流场板体的所述第一引导墙的长度大于所述流场板的所述第二引导墙的长度,以允许所述支撑板被设置在所述第一引导墙。A fuel cell according to claim 52, wherein said first guide wall of said flow field plate of said flow field plate has a length greater than a length of said second guide wall of said flow field plate to allow The support plate is disposed at the first guide wall.
  62. 根据权利要求53所述的燃料电池,进一步包括至少一个密封垫,其中所述密封垫为一空心结构,且所述密封垫的密封部分被设置在前一个流场板的所述流场板体的所述阳极侧的周缘和后一个流场板的所述支撑板的所述连续密封平面之间,其中所述膜电极组的周缘被设置在所述密封垫的密封部分与前一个流场板的所述流场板体的所述连续密封平面之间,从而使得前一个流场板的所述流场板体、后一个流场板的所述支撑板和所述膜电极组形成一个密封空间,以用于燃料流动。A fuel cell according to claim 53, further comprising at least one gasket, wherein said gasket is a hollow structure, and a sealing portion of said gasket is disposed in said flow field plate of said previous flow field plate Between the circumference of the anode side and the continuous sealing plane of the support plate of the latter flow field plate, wherein the periphery of the membrane electrode set is disposed at a sealing portion of the gasket and a previous flow field Between the continuous sealing planes of the flow field plate of the plate such that the flow field plate of the previous flow field plate, the support plate of the latter flow field plate and the membrane electrode group form a Seal the space for fuel flow.
  63. 根据权利要求62所述的燃料电池,其中所述密封垫的两端被分别设置在前一个流场板的所述流场板体的所述端部和相应的后一个流场板的所述支撑板的所述端部之间,其中所述密封垫被设置分别围绕前一个流场板的所述流场板体的两个第二连通开口和后一个流场板的所述支撑板的两个第一连通开口,从而使得当所述燃料电池被组装和所述密封垫被挤压在两个流场板之间时,前一个流场板的所述流场板体和后一个流场板的所述支撑板被密封地相互堆叠在一起,以防止燃料自前一个流场板的所述流场板体和后一个流场板的所述支撑板之间的空隙泄漏。A fuel cell according to claim 62, wherein both ends of said gasket are respectively disposed at said end of said flow field plate of said previous flow field plate and said corresponding one of said subsequent flow field plates Between the ends of the support plate, wherein the gasket is disposed to surround the two second communication openings of the flow field plate of the previous flow field plate and the support plate of the latter flow field plate Two first communication openings such that when the fuel cell is assembled and the gasket is squeezed between the two flow field plates, the flow field plate and the latter flow of the previous flow field plate The support plates of the field plates are sealedly stacked one on another to prevent leakage of fuel from the gap between the flow field plate of the previous flow field plate and the support plate of the latter flow field plate.
  64. 根据权利要求53、54、55、56、57、58、59、60、61、62或63所述的燃料电池,其中所述支撑板由不导电刚性材料制成。 A fuel cell according to claim 53, 54, 55, 56, 57, 58, 59, 60, 61, 62 or 63, wherein said support plate is made of a non-conductive rigid material.
PCT/CN2016/088556 2016-04-21 2016-07-05 Pem fuel cell stack, and flow field plate assembly for same WO2017181533A1 (en)

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CN201620337978.1 2016-04-21
CN201610250337.7 2016-04-21
CN201620337978.1U CN205828543U (en) 2016-04-21 2016-04-21 Fuel cell and flow-field plate group thereof
CN201610250337.7A CN105870476B (en) 2016-04-21 2016-04-21 PEM fuel cell heap and its flow field board group

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CN101853953A (en) * 2009-04-03 2010-10-06 中兴电工机械股份有限公司 Fuel cell structure with composite polar plates and composite polar plate structure thereof
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