Classifications

• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
  • H01M8/04223—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
  • H01M8/04225—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells during start-up
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/02—Details
  • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
  • H01M8/0267—Collectors; Separators, e.g. bipolar separators; Interconnectors having heating or cooling means, e.g. heaters or coolant flow channels
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/02—Details
  • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
  • H01M8/0258—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
  • H01M8/026—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant characterised by grooves, e.g. their pitch or depth
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/02—Details
  • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
  • H01M8/0258—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
  • H01M8/0263—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant having meandering or serpentine paths
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/10—Fuel cells with solid electrolytes
  • H01M8/1004—Fuel cells with solid electrolytes characterised by membrane-electrode assemblies [MEA]
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
  • H01M8/241—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
  • H01M8/2465—Details of groupings of fuel cells
  • H01M8/2483—Details of groupings of fuel cells characterised by internal manifolds
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/10—Fuel cells with solid electrolytes
  • H01M2008/1095—Fuel cells with polymeric electrolytes
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M2250/00—Fuel cells for particular applications; Specific features of fuel cell system
  • H01M2250/20—Fuel cells in motive systems, e.g. vehicle, ship, plane
• • Y—GENERAL 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
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
  • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
  • Y02E60/30—Hydrogen technology
  • Y02E60/50—Fuel cells
• • Y—GENERAL 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
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
  • Y02T90/00—Enabling technologies or technologies with a potential or indirect contribution to GHG emissions mitigation
  • Y02T90/40—Application of hydrogen technology to transportation, e.g. using fuel cells

Definitions

• the invention relates to a bipolar plate for a fuel cell, a fuel cell with such a bipolar plate and ei motor vehicle having such a fuel cell.
• Fuel cells use the chemical transformation of a fuel with oxygen to water to generate electrical energy.
• fuel cells contain as a core component, the so-called membrane electrode assembly (MEA for membrane electrode assembly), which is a composite of an inone-conducting, in particular proton-conducting membrane and in each case one on both sides of the membrane arranged electrode (anode and cathode).
• MEA membrane electrode assembly
• the fuel in particular hydrogen H 2 or a hydrogen-containing gas mixture, is fed to the anode, where an electrochemical oxidation takes place with release of electrons (H 2 -> 2 H + + 2 e " ).
• the protons H + are transported from the anode space into the cathode space (water-bound or anhydrous) .
• the electrons e " provided at the anode are supplied to the cathode via an electrical line.
• the cathode is supplied with oxygen or an oxygen-containing gas mixture, so that a reduction of the oxygen taking place of the electrons takes place (14 0 2 + 2 e " -> O 2" ).
• these oxygen anions in the cathode compartment react with the protons transported through the membrane to form water (2 H + + O 2 " -> H 2 O).
• the fuel cell is formed by a multiplicity of stacked membrane electrode units whose electrical powers add up.
• a bipolar plate is arranged in each case in a fuel cell stack, which on the one hand serves to supply the process gases to the anode or cathode of the adjacent membrane-electrode assemblies and to dissipate heat.
• Bipolar plates also consist of an electrically conductive material to produce the electrical connection. They thus have the threefold function of the process gas supply of the membrane-electrode units, the cooling and the electrical connection.
• Bipolar plates are known in different designs. Fundamental goals in the design of bipolar plates are the weight reduction, the space reduction, cost reduction and increasing the power density. These criteria are particularly important for the mobile use of fuel cells, for example, for the electromotive traction of vehicles.
• Bipolar plates for fuel cells have a, usually centrally disposed active region, which connects to the catalytic electrodes of the membrane-electrode assembly and where the actual fuel cell reactions take place.
• the active region has on the anode side an open anode gas flow field and on the cathode side an open cathode gas flow field.
• the anode gas and cathode gas flow fields are mostly in the form of channel-like channels.
• open-pore / porous structures are also known (US 201 1/0039190 A1).
• the active region has a closed coolant flow field, which is usually formed in the form of trapped channels.
• bipolar plates In order to supply the active area with the appropriate resources, bipolar plates also have equipment through-openings, namely two anode gas main channels for supply and discharge of the anode gas, two cathode gas main channels for supply and discharge of the cathode gas and two main coolant channels for supply and discharge of the coolant , In the fuel cell stack, these equipment passage openings are congruent to one another, so that they form through the entire stack continuous main supply channels for the corresponding equipment.
• Conventional bipolar plates also have inactive supply regions which substantially serve to connect between the agent ports and the corresponding flow fields of the active region.
• the supply regions each comprise anode gas channels, which are connected in a fluid-conducting manner on the one hand to the anode gas main channel and on the other hand to the anode gas flow field of the active region.
• the inactive supply regions furthermore have cathode gas channels, which are connected in a fluid-conducting manner on the one hand to the cathode gas main channel and on the other hand to the cathode gas flow field of the active region.
• the inactive supply region comprises coolant channels, which are connected on the one hand to the coolant main channel and on the other hand to the coolant flow field in a fluid-conducting manner.
• the operating medium passage openings are each on the two opposite narrow sides of the Bipolar plates arranged, wherein the main coolant channel is positioned in each case substantially between the anode gas main channel and the cathode gas main channel.
• a disadvantage of the known bipolar plates is that very different operating pressures prevail within the anode gas channels and in particular within the anode flow field of the active region.
• corner and edge regions of the active surface of the bipolar plate are often undersupplied.
• This problem of the different anode gas supply of the active area is particularly strong in river fields with interrupted channels to bear, in which the individual anode channels are connected laterally. Due to the high pressure differences, significant crossflows occur within the anode gas flow field and a particularly high inhomogeneity.
• bipolar plates Another problem of the known bipolar plates is product water, which is formed on the cathode side, diffused through the polymer electrolyte membrane and thus reaches the anode side. There, after shutting down the fuel cell at low temperatures, freezing of the water in the anode gas flow field and in the anode gas channels of the service areas occurs. This can lead to clogging of the channel structures, which can not be freed by the comparatively low operating pressure of the anode gas. If such a bipolar plate is used in a fuel cell of a motor vehicle, the water must first be thawed by the coolant after a frost start. As a result, the operational readiness of the fuel cell is delayed.
• US 2007/0202383 A1 discloses addressing the problem of non-uniform anode gas distribution by branching the anode gas channels of the active region of the bipolar plate into different numbers of channels.
• the invention is based on the object of providing a bipolar plate for fuel cells which homogenizes the anode gas supply in the active region of the bipolar plate and has a rapid operational readiness after a cold start.
• the object is achieved by a bipolar plate, a fuel cell with such and a motor vehicle with such a fuel cell with the characteristics of the independent
• the bipolar plate for a fuel cell according to the invention comprises an anode side and a cathode side.
• the bipolar plate has the following with respect to a view of the anode side or the cathode side:
• an active region which forms an open anode gas flow field on the anode side and an open cathode gas flow field on the cathode side and has a closed coolant flow field
• Operating means through-holes, at least comprising two anode gas main channels for supply and discharge of the anode gas, two cathode gas main channels for supply and discharge of the cathode gas, and two main coolant channels for supply and discharge of the coolant,
• - two inactive service areas comprising anode gas channels each fluidly connected to one of the anode gas main channels and the anode gas flow field of the active area; Cathode gas channels each fluidly connected to one of the cathode gas main channels and the cathode gas flow field of the active region; and coolant passages respectively fluidly connected to one of the main coolant channels and the coolant flow field of the active region.
• At least one of the anode gas main channels is arranged and the anode gas channels of the supply region connected to this anode gas main channel are designed such that a length difference between a longest anode gas channel and a shortest anode gas channel of the anode gas channels of this supply region is at most 50%, in particular at most 40% and preferably at most 35% based on the length of the longest Anodengaskanals.
• both anode gas main channels are arranged in this way and the anode gas channels of both supply regions are formed in this way.
• the very different channel lengths of the anode gas channels of the supply regions are the cause of the inhomogeneous distribution of the anode gas in the active region of the fuel cell.
• suitable positioning of the anode gas main channels or the anode gas main channels as well as suitable design of the courses of the anode gas channels of the service area it is possible to largely match the lengths of the anode gas channels of the service area and thus to minimize pressure differences within the anode gas channel structures. In this way, a very uniform loading of the active region of the fuel cell is achieved with the anode gas.
• active region is understood to mean that region of the bipolar plate which faces the catalytic electrodes of the membrane-electrode assembly in the assembled fuel cell stack, ie the region at which a fuel cell operates during operation
• inactive region refers to an area where no chemical reaction takes place.
• the “inactive area” includes the inactive coverage areas, the device vias, and edge areas of the bipolar plate It is understood that the bipolar plate is not chemically active in any of the areas in the narrower sense.
• a particularly simple possibility for achieving such an approximation of the channel lengths of the anode gas channels consists in an arrangement of the anode gas main channel substantially between one of the cathode gas main channels and one of the coolant main channels.
• both anode gas main channels are each arranged between a cathode gas main channel and a coolant main channel.
• a main channel for the anode gas, the cathode gas and the coolant are preferably arranged in each case substantially along one side of the bipolar plate, in particular a narrow side of the bipolar plate.
• the cathode gas main channel and the coolant main channel are respectively positioned in the corners of the bipolar plate.
• a profile of the anode gas channels of the supply region has at least one change of direction (deflection) within the supply region.
• a first flow direction of the substantially mutually parallel anode gas channels in the direction of a first side of the bipolar plate has, in particular a longitudinal side thereof, and a second flow direction towards a second, the first side opposite side of the bipolar plate has ,
• the anode gas channels first cross a fictitious main flow direction of the active region of the bipolar plate in one direction then in the other direction.
• a preferred embodiment of the present bipolar plate according to the invention relates to the course of the coolant channels of the service areas. Accordingly, the coolant channels and the anode gas channels of at least one of the two supply regions extend essentially over a congruent section of the bipolar plate. In this way, the Anodengaskanäle be connected virtually thermally well over its entire length to the coolant channels. If it comes to freezing water in the Anodengaskanälen, this can be thawed by the coolant that can be heated during a cold start. Thus, a fuel cell equipped with bipolar plates according to the invention, after a cold start faster ready for use.
• the coolant channels of at least one of the two supply regions in a first section which is connected to the main coolant channel, extend substantially on the cathode side of the bipolar plate.
• the coolant channels extend essentially on the anode side.
• the first section, on which the coolant channels are formed on the cathode side substantially congruent with that section on the anode side, in which the anode gas channels of the supply region extend in the first flow direction.
• the closed coolant channels run parallel and in each case between two anode gas channels.
• the bipolar plate has at least two superimposed, profiled plates, namely an anode-side plate and a cathode-side plate.
• the Anodengaskanäle and Kathodengaskanäle the inactive supply sections are formed by corresponding grooves of the plates or limited by corresponding wall-like elevations (webs).
• the closed coolant channels are formed between the two plates.
• the anode gas flow field and the cathode gas flow field of the active region of the bipolar plate are in the form of straight or meandering flow channels, which are realized as embossed grooves in the respective plate.
• the flow channels can be formed as interrupted channels with particular advantage, thus allowing a transition between two adjacent flow channels. As a result, a particularly homogeneous distribution of the anode gas or cathode gas over the active area is achieved.
• a clear surface of the two anode gas main channels is smaller than a clear surface of the two cathode gas main channels.
• a further aspect of the present invention relates to a fuel cell which has at least two bipolar plates according to the invention, usually a plurality of bipolar plates, and in each case one membrane-electrode unit arranged between two bipolar plates.
• an aspect of the invention relates to a motor vehicle having such a fuel cell, in particular as a power source for an electric motor drive.
• FIG. 1 is a schematic sectional view of a fuel cell (single cell);
• FIG. 2 shows a plan view of an anode side of a bipolar plate according to the prior art
• FIG. 3 partial view of the anode side of a bipolar plate according to the present invention
• FIG. 4 shows a partial view of the anode side of a bipolar plate according to the prior art according to FIG. 2A with a highlighted inactive supply region;
• FIG. 5 partial view of the anode side of a bipolar plate according to the present invention
• FIG. 6 shows an idealized plan view of the anode side of a bipolar plate according to FIG.
• FIG. 7 shows an idealized plan view of the cathode side of a bipolar plate according to the present invention (without active region);
• FIG. 8 shows an idealized plan view of the anode side of a bipolar plate according to FIG.
• FIG. 1 shows a highly schematic sectional view through a fuel cell designated here as a whole by 100, of which only a single cell is shown here.
• the fuel cell 100 comprises a membrane-electrode unit (MEA) 10.
• the MEA 10 has an ionically conductive, in particular proton-conducting polymer electrolyte membrane (PEM) 1 1 on.
• PEM polymer electrolyte membrane
• the PEM 1 1 is contacted by two catalytic electrodes, namely an anode 12 and a cathode 13 surface.
• the electrodes 12, 13 are usually an electrically conductive carrier material, for example based on carbon, on which a catalytic material is present in finely distributed form.
• the area where the electrodes 12, 13 are present and, consequently, the fuel cell reactions take place is referred to as the active area. In an inactive, lateral area are usually no Instead, the membrane 1 1 is mechanically supported there by support layers 14.
• GDL gas diffusion layer
• the GDLs 15 are made of a porous, electrically conductive material and serve to uniformly distribute the anode and cathode operating gases.
• the electrodes 12, 13 may be present as a coating on the PEM 1 1 or the GDLs 15.
• a lateral sealing of the cell via circumferential seals 16 which are arranged on the support layers 14.
• the membrane-electrode unit 10 is arranged between two bipolar plates 20.
• Each bipolar plate 20 has an anode side 21 and a cathode side 22.
• an open anode gas flow field for example in the form of open channels, is arranged in the active region of the bipolar plate 20 (not shown in this illustration).
• a cathode gas flow field is present on the cathode side 22 of the bipolar plates 20, which in turn may be in the form of open channels (not shown).
• the bipolar plates 20 have a closed coolant flow field, likewise not shown, which serves to cool the fuel cell.
• the individual channel structures of the bipolar plates 20 are not shown in FIG. 1, but will be explained in more detail with reference to the following figures.
• a fuel cell comprises a stack of a plurality of membrane-electrode assemblies 10 and bipolar plates 20, which are alternately stacked and their electrical powers add up.
• the fuel cell 100 of FIG. 1 has the following function:
• an anode gas - in this case hydrogen H 2 - fed and fed via the gas diffusion layer 15 of the anode 12.
• the hydrogen reacts to protons H + with the release of electrons which are supplied to the cathode 13 via an external circuit.
• the protons formed at the anode 12 diffuse over the proton-conducting polymer electrolyte membrane 1 1 and reach the cathode 13.
• a cathode gas - here air - fed which fed via the gas diffusion layer 15 of the cathode 13 becomes.
• FIG. 2A shows a prior art bipolar plate 20 'according to US 2006/0127706 A1.
• the bipolar plate 20 ' is shown here in plan view on its anode side 21.
• Figure 2B shows a more detailed example of the upper, inactive region of the bipolar plate 20 'of Figure 2A.
• the bipolar plate 20 ' has a central active region 23 in which an anode-side open anode gas flow field 24 is formed, here in the form of open meandering channels 24.
• an open cathode gas flow field with corresponding channels is formed on the cathode side not visible here.
• a closed coolant flow field in the form of internal, ie closed coolant channels which are likewise not visible in the present case.
• the bipolar plate 20 ' also has two inactive supply regions 26a and 26b.
• the supply regions 26a, 26b each have open anode gas channels 28 which are fluidly connected to the channels 25 of the anode gas flow field 24.
• the anode gas channels 28 extend directly and rectilinearly in a direction oblique to the main flow direction of the active region 23.
• the inactive supply regions 26a and 26b have open cathode gas channels on the cathode side, which is not visible here, of the bipolar plate 20 ', which are connected in a fluid-conducting manner to the likewise not visible cathode flow field of the active region 23.
• the cathode gas channels of the supply regions 26, a, 26b Similar to the anode gas channels 28, the cathode gas channels of the supply regions 26, a, 26b also run in a straight line and in a direction oblique to the main flow direction of the active region 23. Finally, the inactive supply regions 26a and 26b have closed coolant channels 30 (visible here as wall-like elevations), which are connected in a fluid-conducting manner to the coolant flow field of the active region 23.
• the bipolar plate 20 also has a total of six equipment through-openings. These include two anode gas main channels 31 a, 31 b, two cathode gas main channels 32 a, 32 b and two main coolant channels 33 a and 33 b. Of these, one opening of the supply of the respective operating means and the other opening of the discharge of the same serves in each case.
• the open anode gas channels 28 of the inactive supply region 26a connect the anode main gas channel 31a to the open channels 25 of the anode gas flow field 24 of the active region 23.
• the open anode gas channels 28 of the inactive supply region 26b connect the anode main gas channel 31b to the other side of the anode Anode gas flow field 24 of the active region 23.
• the non-visible cathode open gas channels of the supply region 26a connect the cathode gas main channel 32a to the cathode gas flow field of the active region 23 and the cathode gas channels of the supply region 26b connect the cathode gas main channel 32b to the cathode gas flow field.
• the bipolar plate 20 'further comprises a centering opening 34 which the orientation of the bipolar plates in assembly of the fuel cell stack is used.
• the anode gas channels 28 and cathode gas channels of the supply regions 26a and 26b are here each formed as (outwardly) open channels. They are usually covered in the assembled state of the fuel cell stack by the support layer 14 of the membrane electrode assembly 10 and closed (see Figure 1). Alternatively, however, the anode and cathode gas channels of the supply regions 26a and 26b may also already be formed closed in the unassembled bipolar plate.
• the open anode gas channels 28 of the inactive supply region 26a have a significant length difference between the maximum and the shortest anode gas channels 28 of the supply region 26a.
• the channel length of the shortest channel (far left in the illustration) is approximately 5 mm and the channel length of the longest anode gas channel (on the right in the illustration) is approximately 150 mm. This corresponds to a length difference of about 97% with respect to the longest anode gas channel 28.
• This large difference in length results in a significant difference in pressure drop between the shortest and longest anode gas channels 28. This results in uneven supply to the channels 25 of the anode gas flow field 24 of the active region 23.
• bipolar plate 20 which is shown in the form of a preferred embodiment in FIG. In this case, similar to the representation according to FIG. 2B, only the anode side 21 of the upper inactive region 26a of the bipolar plate 20 is shown.
• Like elements are denoted by the same reference numerals. Furthermore, unless otherwise stated, the same elements have the same functions and constructions as in FIG.
• the bipolar plate 20 according to the invention according to FIG. 3 has an arrangement of the device through-openings 31, 32 and 33 deviating from the known bipolar plate 20 '(see FIG. Specifically, here, the anode gas main passage 31 a is disposed substantially between the cathode main gas passage 32 a and the main coolant passage 33 a, that is, the main passage 31 a. H. of the
• Cathodic gas main channel 32a and the main coolant channel 33a are arranged substantially in corner regions, in particular the short sides, of the bipolar plate 20. Furthermore, the profile of the anode gas channels 28 of the supply region 26a has a change of direction (deflection) within the supply region 26a. In this case, a first flow direction A of the anode gas channels 28 in the region of the supply region 26a points in the direction of a first side of the bipolar plate 20, in particular the longitudinal side of the plate shown on the left. Then, the flow channels 28 are deflected, here for example by an angle of 90 °, so that they have a second flow direction B.
• the second flow direction B points in the direction of a second side opposite the first side of the bipolar plate 20, in this case in the direction of the right longitudinal side of the plate 20.
• This selection of the courses of the anode gas channels 28 ensures that the length difference between the longest anode gas channel (left in FIG. 3) and the shortest anode gas channel (on the right in FIG. 3) is significantly reduced compared with the prior art.
• the length of the longest anode gas channel 1 is 15 mm and that of the shortest is 80 mm. This corresponds to a length difference of approximately 30% with respect to the longest anode gas channel 28.
• the arrangement and configuration of the agent passage openings 31b, 32b and 33b and the anode gas channels 28 of the second inactive supply area 26b are preferably designed in the same way as in the area 26a.
• the bipolar plate 20 according to the invention is further distinguished by the design of the coolant channels 30 in the supply regions 26a, 26b. As will be seen from FIGS. 6 to 8, in particular FIG.
• the closed coolant channels 30 of the supply regions 26a and 26b extend in a first section, which is connected to the corresponding main coolant channel 33a, 33b, essentially on the cathode side 22.
• the region on which the coolant channels 30 of the supply region 26a, 26b run on the cathode side 22 of the bipolar plate 20 substantially corresponds to that region of the supply region 26a, 26b in which the anode gas channels 28 extend in the first direction A.
• the cathode-side course of the coolant channels 30 ends and is continued with coverage on the anode side 21.
• the coolant channels 30 of the supply regions 26a, 26b thus run on the anode side 21 of the bipolar plate 20.
• the course of the coolant channels 30 on the anode side 21 of the plate 20 corresponds to that of the anode gas channels 28, d. H.
• the coolant channels 30 are guided parallel to the anode gas channels 28 in this area. They thus also have the second flow direction B of the anode gas channels 28 in this area.
• the coolant channels 30 are arranged in this second section so that they each extend between two anode gas channels 28.
• This embodiment of the courses of the coolant channels 30 ensures that they extend in the coverage areas 26a, 26b essentially in a congruent section of the bipolar plate 20 with the anode gas channels 28.
• a good thermal connection of the anode gas channels 28 to the coolant channels 30 of the supply regions 26a, 26b is achieved.
• the anode gas channels 28 are already thermally coupled to the coolant at the beginning of their entry from the anode gas main channel 31 a, 31 b.
• a cold start of the fuel cell a rapid thawing of the water is achieved by the warmer or heated coolant.
• the fuel cell is ready for use faster after a cold start. Is on the other side in the Kathodengaskanälen 29 of the supply areas 26a, 26b Frozen water present, this is due to the heated by the high compression cathode gas (air) heated and thawed anyway anyway.
• the bipolar plate 20 according to the invention also leads to a smaller dimensioning of the plate, since the existing plate surfaces are optimally utilized for accommodating the anode gas channels 28, cathode gas channels 29 and coolant channels 30 of the supply regions 26a and 26b. While in the bipolar plate of Figure 2B, a portion of the area of the supply areas 26a and 26b is always used on one side only for the anode gas and cathode gas channels 28, 29, the available area of the inactive supply area 26a, 26b on both sides of the plate 20 for the various channels 28, 29 and 30 of the resources used. This situation is visualized in FIGS.
• the area of the inactive supply area 26a of the bipolar plate 20 according to the invention is approximately 4,400 mm 2 (FIG. 5), while the area of the inactive area 26a of the conventional bipolar plate 20 'is 5,494 mm 2 (FIG. 4).
• the clear diameters of the main operating channels 31 a, 32 a and 33 a are unchanged.
• the reduction of the inactive supply region 26a, 26b allows a significant reduction in the dimensions of the bipolar plate 20. In this way, not only the necessary space for the fuel cell, but also their weight is significantly reduced.
• FIG. 6 shows a bipolar plate 20 according to the invention from its anode side 21 and FIG. 7 from its cathode side 22.
• FIG. 8 shows a superimposition of both views so that, regardless of their actual visibility, both the anode gas channels 28, the cathode gas channels 29 and the coolant channels 30 of the inactive supply regions 26a and 26b are visible.
• the inactive region of the bipolar plate 20 is shown, while the active region 23 with the anode gas flow field 24 or the cathode gas flow field 36 is not further developed.
• FIG. 7 which shows the cathode side 22 of the bipolar plate 20
• the cathode gas channels 29 of the inactive supply regions 26a and 26b have a straight course between the cathode gas main channels 32a, 32b and the cathode gas flow field 35 of the active region 23. They thus largely correspond to the course of conventional bipolar plates.
• the optimal area utilization of the inactive supply areas 26a, 26b is particularly clear from FIG.
• this illustration shows that the coolant channels 30, which are connected to the main coolant channels 33a and 33b, and the Anodengas- channels 28, which are connected to the anode gas main channels 31 a and 31 b, claim a largely congruent area of the bipolar plate 20, wherein this substantially corresponds to the area of the inactive service areas 26a and 26b.

Landscapes

• Life Sciences & Earth Sciences (AREA)
• Engineering & Computer Science (AREA)
• Manufacturing & Machinery (AREA)
• Sustainable Development (AREA)
• Sustainable Energy (AREA)
• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Electrochemistry (AREA)
• General Chemical & Material Sciences (AREA)
• Fuel Cell (AREA)

Priority Applications (2)

Applications Claiming Priority (2)

Publications (1)

Family

ID=50513240

Family Applications (1)

Country Status (4)

Cited By (3)

Families Citing this family (12)

Citations (3)

Family Cites Families (12)

• 2013
  • 2013-06-06 DE DE102013210542.8A patent/DE102013210542A1/de not_active Ceased
• 2014
  • 2014-04-15 JP JP2016517197A patent/JP6472439B2/ja not_active Expired - Fee Related
  • 2014-04-15 WO PCT/EP2014/057638 patent/WO2014195052A1/de not_active Ceased
  • 2014-04-15 US US14/895,430 patent/US10230117B2/en active Active

Patent Citations (3)

Also Published As

Similar Documents

Legal Events