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
  • H01M8/02—Details
  • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
  • H01M8/0204—Non-porous and characterised by the material
  • H01M8/0206—Metals or alloys
• • 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
• • 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
  • H01M8/0204—Non-porous and characterised by the material
  • H01M8/0206—Metals or alloys
  • H01M8/0208—Alloys
  • H01M8/021—Alloys based on iron
• • 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
  • H01M8/0204—Non-porous and characterised by the material
  • H01M8/0223—Composites
  • H01M8/0228—Composites in the form of layered or coated products
• • 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
• • 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
  • H01M8/02—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
  • H01M8/0297—Arrangements for joining electrodes, reservoir layers, heat exchange units or bipolar separators to each other
• • 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
  • H01M8/02—Details
  • H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
  • H01M8/028—Sealing means characterised by their material
  • H01M8/0282—Inorganic material
• • 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

Definitions

• the present invention relates to ion exchange polymer membrane fuel cells. More particularly, it relates to the fluid distribution plates used in such fuel cells, such as bipolar plates installed between each of the elementary electrochemical cells and the end plates installed on either side of the stack of cells. different electrochemical cells.
• Bipolar plates used in fuel cells fulfill two very different functions. It is known that the fuel cell and the oxidizing gas, that is to say hydrogen and air or pure oxygen, must be fed to the cell, and that it must also be cooled, that is to say pass through a cooling fluid such as water. One of the functions of the bipolar plates is to allow the transport of these various fluids necessary for the operation of the fuel cell. In addition, the bipolar plates also fulfill an electrical function: to ensure the electrical conduction between the anode and the cathode of each of the adjacent electrochemical cells. Indeed, a fuel cell is always constituted by the series assembly of a large number of elementary electrochemical cells; the elementary electrochemical cells being connected in series, the nominal voltage of the fuel cell is the sum of the voltages of each elementary electrochemical cell.
• bipolar plates must have a very high electrical conductivity.
• the materials used must also be impervious to the fluids used and show a very high chemical stability vis-à-vis these fluids.
• the bipolar plates must have sufficient mechanical characteristics to allow the juxtaposition of a large number of elementary electrochemical cells and associated bipolar plates and the maintenance of the assembly by compression between end plates with tie rods.
• the bipolar plates must have sufficient mechanical characteristics to support this compression.
• Graphite is commonly used because this material offers both high electrical conductivity and is chemically inert to the fluids used.
• Patent application WO 2005/006472 shows a possible embodiment of such bipolar plates.
• the graphite plates comprise the networks of channels necessary for the distribution of fuel and oxidant gases, that is to say in hydrogen and air or pure oxygen, and the network of channels making it possible to cross each bipolar plate by a coolant like water.
• Patent Applications US 2003/0228512 and US 2005/0252892 disclose a bipolar fuel cell plate formed from two plates each formed of a metal substrate having a conductive core region, the conductive region being coated with an ultra-thin layer. of conductive metal, and interposition of a third partition plate. Again, the realization of such a coating obeys the cost price of bipolar plates and the proposed structure is even more complex.
• metal plates as bipolar plates offers several advantages over graphite plates.
• the main advantage to mention is the superior mechanical strength of the metal which makes it possible to reduce the thicknesses of the plates, and to avoid the problems of plate cracks.
• the object of the present invention is to provide a bipolar plate or end plate arrangement which is as easy to manufacture as possible, which achieves very high power output ratios relative to the weight and congestion of the fuel cell, that is to say that allows including cooling by a coolant, to make the use of the fuel cell in a motor vehicle much easier.
• the object of the present invention is to improve the metal bipolar plates, because of their high strength, while eliminating the problem of electrical loss to the second of the two contacts mentioned above.
• the invention provides a fuel cell distribution plate, consisting of the superimposition of a first plate and a second plate, the first plate being made of electrically conductive material and having an inner face and an outer face for to cooperate with an ion exchange membrane, the outer face having a distribution channel network for a first gas, the distribution plate having a second electrically conductive material plate having an outer face and having an inner face for to be applied against the inner face of the first plate, a network of channels for the circulation of a cooling fluid being arranged on the inner face of the first plate or the second plate, or on both, at least the inner faces of the first and second plates being devoid of surface coating, the plates being joined by a layer of an electrically conductive bonding material, said layer being secured to the inner face of each of the first and second plates.
• a suitable technique for joining the first and second plates is solder, preferably at high temperature.
• the invention is of course applicable to bipolar plates, that is to say to plates whose one side forms the anode of an elementary electrochemical cell of a fuel cell and the other side forms the cathode of an adjacent elementary electrochemical cell. But the invention also applies to end plates. In fact, the invention applies whenever one wants to make a distribution plate having an internal network of channels for circulating a cooling fluid. The remainder of the description only deals, in a nonlimiting manner, with a bipolar plate, in which the outer face of the second plate is intended to cooperate with an ion exchange membrane and comprises a network of distribution channels for a gas.
• the electrically conductive material used for the first and second plates is a metallic material.
• a sheet covering all or part of the inner face of each of the first and second plates is used to produce a solder which ensures excellent contact.
• Another advantage is that it provides an optimum seal between the cooling fluid circuit and the outside and between the cooling fluid circuit and the gas circuit (s).
• the invention also extends to a method of manufacturing a steel distribution plate, for fuel cell, said distribution plate comprising a first plate of electrically conductive material having an inner face and having an outer face intended to cooperate with an ion exchange membrane, the distribution plate having a second plate of electrically conductive material having an outer face and having an inner face to be applied against the inner face of the first plate, a network channels for the circulation of a cooling fluid being arranged on the inner face of the first plate or the second plate, or both, of superimposing said first and second plates by interposing a sheet of a bonding material conduct electricity, to heat the assembly obtained up to the melting temperature of the material of lia while maintaining said first and second plates pressed against each other, allowing the assembly to cool and then releasing the holding pressure of the plates to obtain said distribution plate.
• the invention allows the use of stainless steel, a material chemically inert to the fluids used, at least at the surface, more precisely at least for the surface in contact with said fluids. Indeed, it is very important that the surface of the material is not attacked by hydrogen, by oxygen, by the water which is reformed, by any other substance conveyed in the channels, and in particular that the material remains surface inert under severe conditions prevailing in a fuel cell in operation.
• bipolar plate The following describes in detail a bipolar plate.
• the invention is not limited to bipolar plates; it also extends to distribution plates arranged on either side of the stack of elementary cells.
• Figure 1 is an exploded showing the various components of a bipolar plate according to the invention
• Figure 2 is an exploded showing, from another angle of view, the various constituent elements of a bipolar plate according to the invention
• Figure 3 is a perspective showing a bipolar plate according to the invention as it appears when assembled
• Figure 4 is a perspective showing, from another angle of view, a bipolar plate according to the invention as it appears when assembled;
• Figure 5 is an elevational view of one of the outer faces of a bipolar plate according to the invention
• Figure 6 is a section along AA in Figure 5;
• Figure 7 is an enlargement of the portion identified by the circle B in Figure 6;
• FIG. 8 schematically shows an elementary electrochemical cell of a fuel cell using a distribution plate according to the invention. DESCRIPTION OF THE PREFERRED EMBODIMENT OF THE INVENTION
• the first plate 11 and the second plate 12 comprise on one side an area having three openings 31, 32 and 33 of relatively large cross section, and on the opposite side another zone also having three openings 34, 35 and 36 of section relatively important. All the openings 31 are aligned from one plate 11 to the other 12. Similarly, all the openings 32, respectively 33, 34, 35 and 36 are aligned from one plate 11 to the other 12.
• the set of openings 34, respectively 36, form a nurse for the return of one of the gases: the openings 34 and 36 ensure the return (34) of hydrogen not consumed by the battery and the others (36) oxygen not consumed by the battery. All apertures 32 form a feeder which carries the coolant while all apertures 35 form a feeder which returns coolant for regulating the fuel cell temperature.
• One of the faces 11 o of the first plate 11 comprises a first distribution channel 1 1 1 traced to distribute over the entire useful section of the first plate 11 one of the two gases used by the fuel cell.
• the first distribution channel 111 begins with a hole 1 1 1a through the thickness of the first plate 11, and ends with a hole 1 1 1b also passing through the first plate January 1.
• One of the faces 12i of the second plate 12 has an internal channel 122, designed to distribute over the entire useful section of the second plate 12 the cooling fluid used to regulate the fuel cell temperature.
• the coolant may be a liquid or could be air. In the latter case, the fluid passage section should normally be larger.
• the orifice 111a is aligned with the end of a channel section 11 1c dug on the face 12i.
• the orifice 111b is aligned with the end of a channel section 111d dug on the same face 12i.
• Each of these channel sections 111c and 111d communicates with the openings 31 and 34. This ensures communication between the first distribution channel 111 and the nurses concerned.
• the second plate 12 has a second distribution channel 121, similar to the distribution channel 111 and also traced to distribute over the entire useful section of the second plate 12 the other of the two gases used by the fuel cell.
• the openings 33 and 36 of the second plate 12 are in communication with, respectively, a channel section 121c and with a channel section 121d both dug on the face 12i.
• Each of the channel sections 121c and 121d ends with an orifice 121a, respectively 121b, passing through the thickness of the second plate 12, for communicating the second channel 121 with the nipples concerned.
• An advantageous material is stainless steel for distribution plates.
• nickel or copper pure nickel or copper, preferably pure pure is understood as well known to those skilled in the art more than 99% of the element considered- or alloy based on copper or nickel-based alloy).
• Cu-P alloy about 95% copper, the phosphorus balance
• Ni-P alloy 89% Ni and 1% P
• Ni-Cr-Si alloy 71% Ni, 19% Cr and 10% Si
• Ni-B-Cr-Fe-Si alloy (74% Ni, 3% B, 14% Cr, 4.5% Fe and 4.5% Si)
• the solder material is used in paste or preferably in the form of a sheet.
• the solder sheet is cut to the size of the first and second plates.
• An assembly is formed formed by the first plate 11, the second plate 12, with interposition of a solder sheet 2.
• the thickness of this solder sheet is chosen such that the solder, on the one hand, provides electrical contact very uniform between the first and second plates, and secondly, ensure perfect sealing without impeding the smooth flow of heat transfer fluid.
• a typical but non-limiting thickness of this sheet is of the order of one hundredth of a millimeter. Recall that the inner faces 1 1 i and 12i of the first and second plates are free of surface coating.
• This assembly is heated at least up to the melting temperature of the solder metal. Typically, this temperature is exceeded of the order of 10 0 C to 20 0 C to be certain that the entire solder sheet passes into the liquid phase. Of course, the exact temperature is a function of the material chosen for the solder.
• a bipolar plate 1 having on one side of the channels 111, for example anode gas circuit, is obtained on the other side of the channels 121, in this example of the cathode gas circuit, and between the channel plates. 122, not visible after assembly, of the cooling fluid circuit.
• the assembly obtained is heated under a neutral gas atmosphere (for example nitrogen) until a temperature plateau below the melting temperature of the material (for example of the order of 800 ° C. for a copper solder). Then, evacuation is carried out in order to continue the temperature rise, up to about 1100 ° C. for pure copper brazing, more preferably after the temperature rise phase up to the melting temperature of the bonding material, the assembly is allowed to cool under vacuum until a temperature level lower than the melting point of the material (for example the same temperature step as during the temperature rise), and cooling is continued under an atmosphere of neutral gas (for example nitrogen).
• a neutral gas atmosphere for example nitrogen
• a bipolar plate according to the invention is intended to be associated with elements forming an electrochemical cell.
• an electrochemical cell 9 associated with two identical bipolar plates 1A and 1B.
• an electrochemical elementary cell 9 usually consists of the superposition of five layers: a ion exchange polymer membrane 91, two electrodes 92 (only one visible in the drawing) comprising chemical elements necessary for the conduct of the electrochemical reaction, such as for example platinum, and two gas diffusion layers 93 (only one visible in the drawing). ) to ensure a homogeneous distribution of the gases conveyed by the channel networks of bipolar plates over the entire surface of the ion exchange membrane.
• Apertures 31, 32, 33, 34, 35 and 36 are also provided on the polymeric membranes 91 and are aligned with the apertures of the distribution plates.
• Each of the faces 1 1 o and 12 o of the bipolar plates can cooperate with one of the diffusion layers of the electrochemical cells 9 adjacent.
• a large number of electrochemical cells 9 are superimposed with the interposition of bipolar plates 1, and single (non-bipolar) distribution plates are arranged at the ends to form a fuel cell.
• each of the elementary plates an electrically conductive material having sufficient mechanical characteristics to allow not only the transmission of service requirements for the fuel cell, but also to allow the automation of the manufacture of bipolar plates. Indeed, such automation requires manipulations by manufacturing robots and if these manipulations require little precautions thanks to the strength of the constituent material of the base plates, the realization of the automatic manufacturing will be simpler, more robust and more economical.

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• Chemical & Material Sciences (AREA)
• Life Sciences & Earth Sciences (AREA)
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• Sustainable Development (AREA)
• Sustainable Energy (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Electrochemistry (AREA)
• General Chemical & Material Sciences (AREA)
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• 2007
  • 2007-01-09 FR FR0700184A patent/FR2911219B1/fr not_active Expired - Fee Related
  • 2007-12-21 WO PCT/EP2007/011407 patent/WO2008083836A1/fr active Application Filing
  • 2007-12-21 EP EP07857113A patent/EP2122728A1/de not_active Withdrawn
  • 2007-12-21 US US12/522,670 patent/US20100310956A1/en not_active Abandoned
  • 2007-12-21 CN CNA2007800496043A patent/CN101601155A/zh active Pending
  • 2007-12-21 KR KR1020097016527A patent/KR20090108625A/ko not_active Application Discontinuation
  • 2007-12-21 JP JP2009545104A patent/JP2010516027A/ja active Pending

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