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
  • H01M8/0297—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
  • H01M8/02—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
  • H01M8/24—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
• • 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
• • 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
  • H01M8/2418—Grouping by arranging unit cells in a plane
• • 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
  • H01M8/247—Arrangements for tightening a stack, for accommodation of a stack in a tank or for assembling different tanks
  • H01M8/248—Means for compression of the fuel cell stacks
• • 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 an elementary module of a fuel cell and a fuel cell comprising at least one elementary module.
• Two main types of fuel cells are known for generating an electric current by oxidation of a fuel, generally dihydrogen by an oxidant, generally oxygen.
• a first group of cells is formed of "planar" cells as described in FR 3 000 615 A1 and WO 2011/079377 A1.
• Such fuel cells are thin, their lengths and widths being large compared to their respective thicknesses. They are generally fed with oxygen by natural convection and their power is low, limited to 100 W at the most.
• a second group of cells consists of the cells comprising a plurality of thin elementary modules each extending in a longitudinal direction, stacked one on the other and electrically connected in series.
• Each elementary module comprises an oxidation unit formed of an anode and a cathode sandwiching an electrolytic membrane, the oxidation unit being itself sandwiched between bipolar plates ensuring on the one hand the supplying the cathode of an elementary module by means of a flow containing the oxidant and supplying the anode of the adjacent elementary module by means of a flow containing the fuel, and secondly, the electrical connection oxidation units, serving as anodic and cathodic electron collectors.
• WO 2013/134789 A1 describes a fuel cell comprising a compression belt surrounding and compressing an assembly consisting of two end plates sandwiching a stack of elementary modules.
• WO 03/083977 A1 discloses a fuel cell comprising a stack of elementary modules housed in a box having a box and a lid for closing the box, the height of the housing being less than the height of the stack before closing of the box. The box and the lid have complementary reliefs, so that by snapping the lid on the box, compression is applied to the stack.
• the invention proposes, in a first of its aspects, a basic module that is useful for a fuel cell, the elementary module comprising:
• an oxidation unit configured to generate electrons by means of the oxidation of a fuel, preferably dihydrogen, with an oxidant, preferably oxygen, the oxidation unit comprising an anode and a cathode sandwich an electrolytic membrane,
• an anode block comprising a fuel carrier adapted to transport an anode feed stream containing the fuel to an anode chamber, and an anode electron collector attached to the fuel carrier,
• an oxidizing carrier medium suitable for transporting a cathodic feed stream containing the oxidant to a cathode chamber, and a cathodic electron collector fixed on the oxidant carrier,
• the elementary module being shaped so as to define the anode chamber, respectively the cathode chamber, between the oxidation unit and the fuel carrier, respectively the oxidant carrier,
• a battery comprising at least one elementary module according to the first aspect of the invention does not require compression means such as those of the prior art to ensure a good electrical connection between the anode and the anode collector. electrons on the one hand, and between the cathode and the cathodic electron collector on the other hand.
• the anodic and cathodic conductor bridges provide perfect electrical contact between the anodic electron collectors and the cathode electron collector respectively and the oxidation unit.
• the elementary module according to the invention thus has a low total electrical resistance without application of an external compression.
• This low total resistance is partly related to the low internal contact resistances of the elementary module.
• the anodic and cathodic conductor bridges provide, at least partially or completely, the mechanical strength of the elementary module, rigidly connecting the anode and cathode blocks to the electrolysis unit.
• the total mass of the anodic and cathodic conductor bridges is small compared to the mass of the means necessary to ensure the compression of a battery of the same volume and having the same number of elementary modules as a battery of the prior art.
• a battery comprising an elementary module according to the first aspect of the invention has a higher power density.
• the oxidation unit and the fuel carrier can be both bonded to one another and electrically isolated from each other by means of an anodic sealing bridge. containing an electrically insulating and waterproof adhesive,
• the anodic sealing bridge being shaped so that the anode feed stream conveyed to the anode chamber flows substantially from the fuel carrier directly to the anode.
• the anodic sealing bridge can advantageously participate in the mechanical strength of the elementary module.
• the invention further relates, in a second aspect, to a basic module useful for a fuel cell, the elementary module comprising:
• an oxidation unit configured to generate electrons by means of the oxidation of a fuel, preferably dihydrogen, with an oxidant, preferably oxygen, the oxidation unit comprising an anode, a fuel carrier adapted to transport an anode feed stream comprising the fuel to an anode chamber, the module being shaped to define said anode chamber between the anode and the fuel carrier,
• the oxidation unit and the fuel carrier being both bonded together and electrically insulated from each other by means of an anodic sealing bridge containing an electrically adhesive insulating and waterproof,
• the anodic sealing bridge being shaped such that when the anode feed stream is transported to the anode chamber by the fuel carrier, said anode feed stream flows substantially from the fuel carrier directly to the fuel carrier; 'anode.
• a battery comprising at least one elementary module according to the second aspect of the invention does not require compression means such as those of the prior art for sealing the fuel cell.
• the anode sealing bridge ensures that the fuel entering the anode chamber by means of the fuel carrier means reaches the anode while preventing it from leaking out of the anode chamber.
• the total mass of the anode sealing bridges is small compared to the mass of the means necessary to ensure the implementation. compression of a stack of the same volume and having the same number of elementary modules as a stack of the prior art. For a mass identical to that of a battery of the prior art, a battery comprising at least one elementary module according to the second aspect of the invention therefore has a mass density of higher power.
• the oxidation unit may comprise an electrolytic membrane in contact with the anode, the anode being disposed between the anode chamber and the electrolyte membrane and optionally an anode collector layer in contact with a face of the anode. anode disposed opposite the anode chamber.
• the elementary module may comprise a cathode block comprising an oxidizing carrier support adapted for introducing a cathodic feed stream containing the oxidant into a cathode chamber, the oxidation unit comprising a cathode disposed in contact with the electrolytic membrane, the electrolyte membrane being sandwiched between the anode and the cathode,
• the module being shaped to define said cathode chamber between the cathode and the oxidant carrier,
• the oxidation unit and the oxidant carrier are both bonded together and electrically isolated from one another by means of a cathodic fixing bridge containing an electrically adhesive insulating.
• the elementary module may include an anode block having the anode electron collector attached to the fuel carrier, and the cathode block may include a cathode electron collector attached to the oxidant carrier,
• the anode electron collector respectively the cathodic electron collector
• the oxidation unit being both bonded and electrically connected to each other by means of an anodic conducting bridge, respectively a cathodic conductor bridge, containing an electrically conductive adhesive.
• the invention also relates to a fuel cell comprising an elementary module according to any one of the first and second aspects of the invention, or a plurality of elementary modules stacked one on the other in a stacking direction, at least one , preferably all the elementary modules of the plurality being each according to any one of the first and / or second aspects of the invention.
• the invention relates to a fuel cell comprising a plurality of elementary modules stacked on top of each other in a stacking direction, at least one, preferably all the elementary modules of the plurality comprising:
• an oxidation unit configured to generate electrons by means of the oxidation of a fuel, preferably dihydrogen, with an oxidant, preferably oxygen, the oxidation unit comprising an anode and a cathode sandwich an electrolytic membrane,
• an anode block comprising a fuel carrier adapted to transport an anode feed stream containing the fuel to an anode chamber, and an anode electron collector attached to the fuel carrier, a cathode block comprising an oxidizing carrier medium suitable for transporting a cathodic feedstream containing the oxidant to a cathode chamber, and a cathode electron collector fixed on the oxidizing carrier support,
• the at least one elementary module being shaped so as to define the anode chamber, respectively the cathode chamber, between the oxidation unit and the fuel carrier, respectively the oxidant carrier,
• the anode block, respectively the cathode block, and the oxidation unit being fixed to each other, and / or the at least one elementary module being such that prior to assembling the at least one elementary module to the within the plurality of elementary modules of the fuel cell, the anode block, respectively the cathode block, and the oxidation unit are fixed to each other.
• the fuel cell according to the invention does not require compression means to ensure the electrical connection between the elementary modules and the fuel tightness of each elementary module. It therefore has a mass density of power greater than a fuel cell of the same mass of the prior art.
• an elementary module of the fuel cell is not compressed by an external force other than the potential weight of other elementary modules arranged vertically above said elementary module, the change of said elementary module is easy in the case where said elementary module is defective.
• two consecutive elementary modules can be separated from one another in the stacking direction.
• the elementary module can thus be easily extracted from the fuel cell by sliding it in a direction transverse to the direction of the stack.
• the elementary module can be removable.
• two members for example the anode block or the cathode block on the one hand and the oxidation unit on the other hand, are fixed to each other, therefore another member rigidly connects said two members.
• said other member is an adhesive bridge, a screw or a rivet.
• the assembly of two parallel plates held together under the application of a compression force normal to their faces does not define a fixation in the sense of the invention, since the plates can in particular be moved relative to each other as soon as the compression force is removed.
• the anode block, respectively the cathode block, and the oxidation unit are fixed to one another by means of a fixing member arranged, at least partially or completely, between the anode block, respectively the cathode block, and the oxidation unit.
• the fixing member may comprise or be constituted by an electrically conductive adhesive or electrically insulating.
• the fixing member may be fixed by at least one of its faces to the anode block, respectively to the cathode block, and to the oxidation unit. Preferably, it is fixed by two of its faces opposite to each other to the anode block, respectively to the cathode block, and to the oxidation unit.
• the fixing member may be disposed between the anode block, respectively the cathode block, and the oxidation unit and may comprise an electrically conductive adhesive, so as to define an anode conductive bridge, respectively a cathode conductor bridge.
• the fastener may be disposed between the cathode block and the oxidation unit and may include an electrically insulating adhesive, so as to define a cathodic attachment bridge.
• the fastener may be disposed between the anode block and the oxidation unit and may include an electrically insulating adhesive, so as to define an anodic sealing bridge.
• the anode block, respectively the cathode block, and the oxidation unit are adhesively bonded and electrically connected to each other, by means of an anodic conducting bridge or a cathodic conducting bridge respectively. , containing an electrically conductive adhesive.
• the anode block comprises an anode electron collector fixed on the fuel carrier, respectively a cathode electron collector fixed on the oxidant carrier, the anodic conducting bridge and the collector.
• anodic electrons respectively the cathodic conductor bridge and the cathodic electron collector being both bonded and electrically connected to each other.
• the oxidation unit and the fuel carrier are bonded to each other and electrically isolated from each other by means of an anode sealing bridge containing an electrically insulating and fuel-tight adhesive, the anode sealing bridge being shaped such that the anode feed stream conveyed to the anode chamber flows substantially directly from the fuel carrier to the anode.
• the invention relates to an apparatus, especially chosen from a flying object, for example a drone, a bicycle and an electric generator, for example a charger for electrically recharging a set of nomadic devices, said apparatus comprising a fuel cell according to the invention. 'invention.
• the elementary module and the fuel cell according to any of the aspects of the invention described above may furthermore include one or more of the features described hereinafter.
• the elementary module is "planar”, that is to say that it extends generally along a longitudinal plane.
• a planar elementary module is particularly well adapted to form a stack of a fuel cell.
• the elementary module may be "thin”, that is to say that its thickness, defined as the average value of the distances, measured in a direction transverse to the longitudinal plane, between two opposite longitudinal outer faces of the elementary module is at least 50 times smaller, preferably at least 2500 times smaller than the length of the elementary module, measured in the longitudinal plane.
• the length and / or width and / or thickness of the elementary module may be respectively between 10 mm and 500 mm, between 10 mm and 500 mm, and between 0.2 mm and 2 mm.
• the longitudinal outer faces of the opposed elementary module are parallel.
• the oxidation unit when the oxidation block is supplied with fuel and oxidant, the electrons generated by the oxidation unit on the faces of the anodes and cathodes opposite the respective faces facing the membrane, said anodic electrons and cathodic electrons respectively, pass through the anode electron collector and the cathode electron collector respectively.
• the oxidation unit preferably comprises a collector layer anodic, disposed on the face of the anode opposite the face of the anode facing the electrolytic membrane, and / or a cathodic collector layer disposed on the face of the opposite cathode to the face facing the electrolyte membrane .
• the anodic collector layer or the cathodic collector layer is separated from the fuel carrier and the oxidant carrier respectively by the anode chamber and the cathode chamber respectively.
• the anodic collector layer and / or the cathodic collector layer may be in the form of a thin film, preferably of a thickness less than 100 ⁇ , and porous so as to allow the anode feed stream to reach the anode, respectively to the cathode feed stream to reach the cathode.
• the anodic collector layer and / or the cathodic collector layer may be deposited respectively on the anode face and / or on the cathode face by 3D printing or by vacuum deposition, for example chemical vapor deposition, or physical deposition. vapor phase.
• the anode collector layer and / or the cathodic collector layer are formed of a metal, preferably gold.
• the anodic collecting layer may occupy between 50% and 100% of the area of the anode face that it covers and / or the cathodic collector layer may occupy between 50 and 100% of the area of the face of the cathode that it covers.
• anodic and cathodic conductor bridges respectively allow the transfer of anode electrons from the anode to the anode electron collector, and cathodic electrons from the cathode to the cathode electron collector.
• the anodic conductor bridge may be bonded to the anode and / or the anode collector layer and / or to the electrolyte membrane.
• the cathodic conductor bridge can be fixed by bonding on the cathode and / or on the cathodic collector layer and / or on the electrolyte membrane.
• the anodic conducting bridge may be arranged between the anode and the fuel carrier so as to partially define the anode chamber, and in particular at least partially, or totally, a wall of said anode chamber, in particular extending in one direction. cross.
• the cathodic conductor bridge can be arranged between the cathode and the oxidizing carrier carrier so as to partially defining the cathode chamber, and in particular at least partially, or totally, a wall of said cathode chamber, in particular extending in a transverse direction.
• the anodic conducting bridge is sandwiched between the oxidation block and the anode electron collector and / or the cathodic conductor bridge is sandwiched between the oxidation block and the cathode electron collector.
• the anode conductor bridge and / or the cathode conductor bridge cover at least partially, or even integrally, the anode electron collector and / or the cathode electron collector respectively.
• the electron transfer between the anode and the anode electron collector and / or between the cathode and the cathode electron collector is optimal.
• the anodic conducting bridge and / or the cathodic conducting bridge may be of various shapes. They may each be in the form of at least one stud or at least one strip, continuous or discontinuous, or at least one surface extending in two perpendicular directions.
• the pads or strips can form a regular pattern, even periodic.
• the pads may be arranged in a network formed by periodic repetition in two perpendicular directions of a square pattern, and at each vertex of one of the patterns of the network.
• a stud may have a straight prism shape, including a square or rectangular base, or a cylindrical shape of revolution.
• the diameter of the pad, corresponding to the greatest length in a direction perpendicular to the generatrix of the prism, may be between 0.1 mm and 10 mm.
• the anodic conducting bridge and / or the cathodic conductor bridge are in the form of at least one strip, preferably the width of at least one, preferably of each of the strips is between 0.1 mm and 10 mm.
• the ratio of the area of the projection of the anodic conducting bridge to the projection area of the fuel carrier can be between 1% and 50% and / or the ratio of the area of the projection of the cathodic conductor bridge, on the projection area of the fuel carrier, may be between 1% and 50%, said projections being made on the longitudinal plane along which extends the elementary module and in a direction transverse to said plane longitudinal.
• the anodic conducting bridge and / or the cathodic conducting bridge may have a thickness of between 1 ⁇ and 100 ⁇ .
• the anodic conducting bridge may protrude from the face of the anode on which it is arranged and / or the cathode conductor bridge may protrude from the face of the cathode on which it is arranged.
• the space defined between the two portions of the strip and extending between planes parallel to the lateral faces of the strip may be at least partially or even completely filled by an anode isolation bridge, respectively a cathodic insulation bridge.
• the anodic conducting bridge and the anodic isolation bridge may at least partially define a transverse wall of the anode chamber, for example completely encircling the anode chamber, and / or the cathodic conducting bridge and the cathodic insulation bridge may define at least partially a transverse wall of the cathode chamber, for example wholly encircling the cathode chamber.
• the anodic conductor bridge and / or the cathode conductor bridge may be formed on the anode block and / or on the cathode block respectively, or on the oxidation unit by printing an adhesive comprising the electrically conductive adhesive, for example by screen printing, spraying or dispensing.
• the anode conductor bridge and the cathode conductor bridge each contain an electrically conductive adhesive.
• the electrically conductive adhesive may in particular have anisotropic conductivity.
• the anodic conducting bridge, or the cathodic conducting bridge is such that the direction of greater electrical conductivity of the electrically conductive adhesive is parallel to the direction normal to the thickness of the anodic conducting bridge, respectively of the cathode conductor bridge. .
• the electrically conductive adhesive comprises or even consists of a polymer resin in which carbon particles, for example in the form of graphene, and / or metal particles are dispersed.
• the metal particles comprise, or even consist of, a metal chosen from silver, gold and their alloys, or are formed of a metal core, preferably of a metal chosen from copper and nickel and their alloys. covered with a carbon coating or metal coating, preferably of a metal selected from gold, silver and their alloys.
• the electrically conductive adhesive of the anodic conducting bridge may be identical to or different from the electrically conductive adhesive of the cathode conductor bridge.
• the adhesive may be TRA-DUCT 2902 sold by Tra-Con.
• the oxidation unit is preferably disposed between the anode block and the cathode block.
• the oxidation unit extends in a plane parallel to or coincident with the longitudinal plane.
• the oxidation unit may have the form of a composite plate and / or each of the anode, cathode and electrolyte membrane may have the shape of a plate extending in a plane parallel to the longitudinal plane.
• the thickness of the oxidation unit may be greater than or equal to 0.01 mm and / or less than or equal to 0.5 mm.
• the anode and / or the cathode are fixed on the electrolyte membrane, for example by drying an ink deposited by spraying on the anode, respectively the cathode and / or the membrane, and containing catalysts based on platinum carbon (C / Pt).
• the anode may comprise, or even consist of, a mixture of C / Pt and Nafion, and / or the membrane may be at least partially or even entirely formed of Nafion, and / or the cathode may comprise, or even consist of a mixture of C / Pt and Nafion.
• the fuel carrier and the oxidant carrier preferably at least one, preferably both, extend in a plane parallel to the longitudinal plane.
• the fuel carrier and / or the oxidant carrier may each be in the form of a plate.
• Such fuel carrier carriers and / or oxidant carrier carrier are thus simple, fast and inexpensive to manufacture.
• the fuel carrier and the oxidant carrier are shaped to respectively introduce the anode feed stream containing the fuel into the anode chamber and the cathodic feed stream containing the oxidant in the cathode chamber.
• the oxidizing carrier carrier respectively the fuel carrier
• the fuel carrier and / or the oxidant carrier may have holes, for example bores, passing through the fuel carrier and / or the oxidant carrier respectively in their respective thicknesses.
• the fuel carrier and / or the oxidant carrier may each be in the form of a foam having an open and percolating porosity at least in the direction of its thickness.
• the anode feed stream and / or the cathodic feed stream can flow into the thickness of the fuel carrier and / or oxidant carrier respectively.
• the fuel carrier and / or the oxidant carrier are of an electrically insulating material.
• the fuel carrier and the oxidant carrier may comprise or consist of a polymer material, for example thermoplastic, and in particular selected from polyethylene terephthalate PET, polyethylene PE, polycarbonate PC, FR4, Kapton and their mixtures.
• a polymer material for example thermoplastic, and in particular selected from polyethylene terephthalate PET, polyethylene PE, polycarbonate PC, FR4, Kapton and their mixtures.
• the fuel carrier and / or the oxidant carrier may be in the form of a planar grid.
• the face of the gate facing the anode chamber, respectively the cathode chamber is covered at least partially, preferably even completely by an assembly formed of an electrically insulating film and an electrically conductive metal film defining the anode electron collector, respectively the cathode electron collector.
• the electrically insulating film, and optionally the electrically conductive film is porous, so as to allow the transport of the fuel or oxidant according to its thickness.
• the thickness of the electrically insulating film and / or the thickness of the electrically conductive film is between 10 ⁇ and 500 ⁇ .
• the electrically conductive film and the electrically insulating film cover distinct and preferably non-superposed portions of the face of the gate facing the anode chamber or the chamber respectively.
• cathode For example, the cathodic anode conductor bridge is adhesively bonded to the electrically conductive film of the fuel carrier forming the anode electron collector and the cathodic conductor bridge is adhesively bonded to the electrically conductive film of the oxidant carrier carrier forming the cathodic electron collector.
• the anode conductor bridge and / or the cathode conductor bridge are arranged at a distance from the conductive electrically insulating film of the fuel carrier, respectively of the oxidant carrier.
• an anode electron collector and a cathode electron collector are attached, preferably by glueing to the fuel carrier and the oxidant carrier respectively.
• At least one end of the anode electron collector, respectively of the cathode electron collector can protrude, for example laterally, from the elementary module, and be electrically connected to a contact resumption connector, to connect the elementary module to a electrical apparatus or to another elementary module, for example the consecutive elementary module of the stack of elementary modules of a fuel cell comprising a plurality of elementary modules.
• the anode electron collector may be printed on the fuel carrier and / or the cathodic electron collector may be printed on the oxidant carrier, thereby forming an anode block or block cathode.
• the anode block and / or the cathode block thus formed are then in the form of printed circuits, which facilitates the manufacture of the elementary module, and in particular the relative positioning of said fuel carrier and oxidant carrier relative to the oxidation unit during assembly of the constituent elements of the elementary module.
• the anode electron collector and / or the cathode electron collector are at least partially in the form of strips spaced apart from each other, preferably forming a regular or even periodic pattern, for example a grid.
• the band or bands extend laterally in the longitudinal plane, and in particular between two opposite lateral faces of the elementary module.
• the ratio R of the area SA of the projection of the anode electron collector, to the area S of the projection of the fuel carrier is preferably between 0.01 and 0.50, and / or the ratio R 'of the area S' A of the projection of the cathode electron collector, on the area S 'of the projection of the fuel carrier, is between 0.01 and 0.50, said projections being made on the longitudinal plane, and in a direction transverse to said longitudinal plane .
• the ratios R and R ' can be different or equal.
• the anode electron collector protrudes, preferably in a transverse direction, from the face of the fuel carrier, respectively to the thickness of the oxidant carrier support on which it is fixed, the height of said projection being for example equal to the thickness of said anode electron collector, respectively the cathode electron collector.
• the anode electron collector or the cathode electron collector thus at least partially defines a spacer separating the fuel carrier carrier, respectively the oxidant carrier, from the oxidation unit, said spacer defining partially the anodic chamber, respectively the cathode chamber.
• the thickness of the anode electron collector and / or the thickness of the cathode electron collector is less than 100 ⁇ .
• the anode electron collector and / or the cathodic electron collector are preferably metallic, and may comprise, in particular for more than 99.0% of their mass, carbon and / or a metal selected from among silver, tantalum, molybdenum, copper and their alloys. Such a metal or alloy easily conducts the collected electrons on the anode and cathode.
• the anode electron collector and / or the cathode electron collector may comprise a layer formed of said metal, fixed on the fuel-carrying support, respectively on the oxidizing carrier medium, covered by a protective film, and conductor formed of another metal or a layer superposition, each layer being made of a metal different from that of the other layers of the film, said film being able to have a thickness of less than 10 ⁇ .
• the elementary module may comprise an anode isolation bridge and / or a cathodic isolation bridge, the cathodic insulation bridge being formed of at least one electrically insulating material.
• the anode isolation bridge is disposed between the oxidation unit and the anode electron collector. It can be in direct contact with the oxidation unit and with the anode electron collector.
• the cathodic isolation bridge is disposed between the oxidation unit and the cathode electron collector. It can be in direct contact with the oxidation unit and with the cathodic electron collector.
• the anodic isolation bridge and / or the cathodic insulation bridge are in the form of a thin film, for example having a thickness between 1 ⁇ and 100 ⁇ .
• the anode isolation bridge and / or the cathodic isolation bridge are respectively disposed on a portion of the face of the anode electron collector opposite the oxidation unit and / or on a portion of the face of the cathodic electron collector opposite the oxidation unit, said portion or portions being different from portions covered by the anodic conducting bridge and / or by the cathode conductor bridge.
• the anodic isolation bridge respectively the cathodic insulation bridge, thus protects the portion of the face of the anode electron collector, respectively of the cathodic electron collector, not covered by the anodic conducting bridge, or by the conducting bridge respectively. cathode.
• anode insulating bridge and / or the cathodic insulating bridge may be in the form of one or more interrupted strips, pads, in particular forming a regular pattern, such as a grid.
• the anode chamber is preferably disposed between the fuel carrier carrier, respectively the oxidant carrier, and the oxidation unit.
• the anode chamber and / or the cathode chamber extend in a plane parallel to the longitudinal plane.
• the anode chamber is defined at least partially or completely by:
• the anode chamber is shaped such that when fueled, the fuel pressure in the chamber is greater than the pressure atmospheric, which makes it possible to ensure an efficient oxidation reaction of the fuel at the level of the oxidation unit.
• the anode sealing bridge defines a fuel seal extending transversely to the longitudinal plane between the anode block and the oxidation unit and encircling, preferably integrally, the anode chamber in a plane parallel to the longitudinal plane. In this way, the anodic sealing bridge reduces leakage of fuel out of the anode chamber by fluid flow in directions contained in the longitudinal plane.
• the anodic conducting bridge and / or the anodic sealing bridge are shaped so as to avoid the delamination of the oxidation unit of the anode block, when the fuel pressure is between 0.1 bar and 5 bar.
• Those skilled in the art can easily determine the properties of the electrically insulating and fuel-tight adhesive and / or the electrically conductive adhesive and define the dimensions of the anode conductor bridge and / or the anode sealing bridge for this purpose.
• the anodic sealing bridge is adhesively bonded to the anode and / or the anodic collector layer and / or the electrolyte membrane.
• the anodic sealing bridge may in particular be obtained by printing an adhesive comprising the electrically insulating adhesive and sealed to the fuel, in particular by screen printing, or spraying or dispensing or postponing an adhesive film.
• the electrically insulating and fuel-tight adhesive may in particular be chosen from adhesives such as polyurethane or epoxy type.
• adhesives such as polyurethane or epoxy type.
• it may be the 1RS 2125 glue marketed by Intertronics.
• the anodic sealing bridge can have various shapes. It is preferably in the form of a continuous strip, preferably closed on itself and in contact with each of the opposite longitudinal faces of the anode chamber.
• the elementary module may comprise a reservoir having an interior volume for containing the fuel, the anode chamber being in fluid communication with the interior volume of the tank by means of the fuel carrier.
• the tank defines a fuel reserve for ensuring fuel supply of the anode chamber.
• the fuel carrier means defines a wall of the tank.
• the reservoir and the fuel carrier may form a monolithic block.
• the reservoir comprises a filling orifice shaped to be connected, for example by means of a conduit, to a fuel supply pump or to a fuel-generating cartridge, for example to a hydrogen-generating cartridge. by hydrolysis of hydrides.
• the assembly formed by the internal volume of the reservoir and the volume of the anode chamber is hermetically sealed and sealed with fuel.
• the oxidant carrier and the oxidation unit can be both bonded together and electrically isolated from each other at the same time.
• the electrically insulating adhesive of the cathodic fixing bridge may be the same as or different from the electrically insulating adhesive of the anodic sealing bridge.
• the cathodic fixing bridges and / or cathodic conducting bridge ensure at least partially, preferably integrally, the mechanical strength of the connection between the carrier carrier and the oxidant and the electrolysis unit.
• the cathodic fixing bridge can define a transverse wall of the cathode chamber, which can be closed on itself so as to define an oxidant seal, or on the contrary have openings, so as to facilitate the flow of oxidant out of or to the cathode chamber.
• the elementary module may comprise a plurality of electrolysis units sharing the same electrolytic membrane and preferably being arranged in a planar arrangement. Alternatively, it may comprise a single electrolysis unit.
• the elementary module may also include a gas diffusion layer, preferably disposed on one side of the oxidant carrier opposite to the opposite side of the anode chamber, and covered with a porous grid.
• the gas diffusion layer and the grid contribute to the maintenance of a humidity level adapted to the generation of electricity.
• the gas diffusion layer can be electrically insulating or electrically conductive on the contrary. It can be hydrophilic or, on the contrary, hydrophobic.
• the porous grid may be metallic, and optionally covered with an electrically insulating material, or plastic.
• the elementary module can be configured to generate an electrical power of between 1 W and 500 W.
• the mass of the elementary module may be between 1 g and 1000 g.
• each elementary module of the plurality of modules extends in an oblique longitudinal plane, preferably perpendicular to the stacking direction.
• the elementary modules of the battery can be electrically connected together in series or in parallel.
• the stack may include at least two, at least ten, at least twenty elementary modules.
• the fuel cell is free of compression means of the plurality of elementary modules.
• the fuel cell may be free of end plates disposed at opposite ends of the stack and in particular connected by at least one compression member.
• the stack may comprise a frame in the form of a shelf comprising a plurality of bins arranged one after the other in the stacking direction, each bin extending in a plane transverse to the stacking direction .
• at least one or even more preferably several bins are configured to each house at least one elementary module.
• at least two consecutive modules of the stack can be separated from each other. In this way, the elementary modules of the stack do not rest on each other, the weight of each elementary module being supported by the frame. The replacement of a defective elementary module is thus facilitated.
• the elementary modules may be spaced apart from each other in the stacking direction, regularly, in particular periodically.
• At least two consecutive modules of the stack are arranged head to tail in the stacking direction.
• this arrangement makes it possible to limit the number of members necessary to feed the stack of elementary modules with fuel and / or oxidant.
• the battery may comprise at least one means for generating the oxidant feed stream, and optionally means for generating the means fuel supply, so as to ensure the generation of electrical energy by the at least one elementary module. It may also comprise at least one means, for example a fan, for generating a cooling flow, so as to recover by convective heat exchange generated by the at least one elemental module during the fuel oxidation reaction.
• the cell is shaped to define at least one cathode feed channel configured to transport the cathodic feed stream containing the oxidant to at least one elementary module, and / or at least one cooling channel configured to transporting a cooling stream comprising a heat transfer fluid, preferably air, so as to exchange heat by convection with the at least one elementary module.
• a cathode feed channel configured to transport the cathodic feed stream containing the oxidant to at least one elementary module
• / or at least one cooling channel configured to transporting a cooling stream comprising a heat transfer fluid, preferably air, so as to exchange heat by convection with the at least one elementary module.
• the cathode feed channel and / or the cooling channel may have a tubular shape, extending in a direction contained in a plane parallel to the longitudinal planes along which the elementary modules between which the channel is arranged extend. cathode power supply and / or the cooling channel respectively.
• the cathode feed channel is defined by two side faces, preferably parallel to the stacking direction, opposite the stack and the side faces facing the elementary modules between which said channel is disposed.
• the pressure drop associated with the tubular form of the cathode supply channel and / or the cooling channel is small and the fuel cell can be devoid of means for generating the cathode feed stream and / or the cooling stream respectively .
• the cathode supply channel and / or the cooling channel may have a shape comprising a plurality of tube portions connected by bent portions.
• the tube portions may, for example, go back and forth between the opposite side faces of the stack.
• Such bent shapes particularly promote heat exchange in the cooling channel.
• the cathode feed channel and / or the cooling channel may each be formed of a plurality of coils extending between the inlet and outlet openings of said cathode feed channel and / or said feed channel. cooling respectively, the coils being parallel to each other.
• the cathode feed channel is formed of a plurality of tubes, two neighboring tubes sharing a common wall.
• the tubes of the plurality may be parallel to each other and be arranged between the facing faces of two consecutive elementary modules.
• Such forms of cathodic feed channel and / or cooling channel favor oxidant feed and / or heat exchange respectively.
• the fuel cell may comprise a flow generator. cathode supply and / or a cooling flow generator respectively, preferably comprising a compressor.
• cooling flow generator and / or the cathodic power supply generator may be chosen from a fan, in particular an axial or radial fan, a turbine and a compressor.
• the cathodic feed stream is preferably a stream of air.
• the cooling flow generator and / or the cathodic power supply generator can operate in extraction or air blast, continuous mode or pulse width modulation mode (or "PWM" for the acronym for Maise Width Modulation).
• the battery may comprise one or more cooling flow generators and / or a single or several cathodic power supply generators.
• the fuel cell may comprise a plurality of cooling flow generators such that each of the generators of the plurality feeds a single pair formed by two elementary modules.
• the at least one elementary module is disposed between the cathode supply channel and the cooling channel.
• the cathode feed channel extends in an oblique direction of extension, preferably orthogonal, to the extension direction in which the cooling channel extends.
• the planes along which the cathode supply channel and the cooling channel generally extend are distinct and parallel, and preferably perpendicular to the stacking direction.
• the cathode feed channel has at least one inlet opening, respectively at least one outlet opening, for the inlet flow, respectively at the stack outlet of the cathode feed stream, and the inlet channel.
• cooling device has at least one inlet opening, respectively at least one outlet opening, for inlet flow, respectively at the stack outlet of the cooling flow, the inlet openings and outlet openings of said cathode feed channels; and cooling channels being shaped such that the input and output cathode feed streams flow in at least one oblique direction, preferably perpendicular, to the at least one direction of flow of the inlet cooling streams and stack outlet.
• the inlet openings and outlet openings of said cathode supply and cooling channels are shaped so that the flow direction or directions of the input and output cathode feed streams and the direction or directions of flow of the cooling streams are contained in separate and parallel planes, and preferably perpendicular to the stacking direction.
• the inlet openings and outlet openings of said cathode supply and cooling channels may be of various shapes. For example, they have a circular outline, or rectangular, or square, or oval.
• cooling channel and / or the cathode feed channel may have a plurality of inlet openings and / or a plurality of outlet openings.
• the shape and / or dimensions of the inlet opening of the cooling channel may be the same as or different from the shape and / or dimensions of the outlet opening of the cooling channel.
• the shape and / or dimensions of the cathode feed channel inlet opening may be the same as or different from the shape and / or dimensions of the outlet opening of the cathode feed channel.
• the shape and / or dimensions of the inlet and outlet openings of the cooling channel may be identical or different from the shape and / or dimensions of the inlet and outlet openings of the cathode feed channel.
• the cathode feed channel may be disposed between the respective cathode blocks of at least two consecutive elementary modules of the plurality of elementary modules in the stacking direction, and be shaped to transport the cathode feed stream to the oxidant carrier carrier of each of said two respective elementary modules
• / or the cooling channel may be disposed between at least two consecutive elementary modules of the plurality of elementary modules in the stacking direction and is shaped to carry the flow cooling so as to exchange heat by convection with said two elementary modules.
• a cathodic power supply channel can supply a plurality of elementary modules and / or a cooling channel can exchange heat with several elementary modules. This limits the mass of oxidant supply means and cooling means of the fuel cell.
• the fuel cell preferably comprises:
• each cathodic power supply channel being shaped to supply at least one elementary module with cathodic power supply flux
• a cathode power supply probe arranged in a channel of the plurality of cathode supply channels and configured to measure at least one cathodic power supply property selected from moisture, temperature and pressure,
• a cathodic power supply generator configured to generate the cathodic power stream to be carried in said channel or in another channel of the plurality of cathodic power supply channels
• control unit of said cathode power supply generator configured to adjust, as a function of the measurement of the cathodic power supply property, at least one parameter of said cathode power supply stream to be transported in said channel and / or said stream; cathodic power supply to be carried in the other channel.
• the at least one parameter of said cathode power supply stream may be selected from temperature, pressure, flow rate, cathodic power feed rate at the output of the cathode feed stream generator, and combinations thereof.
• the fuel cell comprises: a plurality of cooling channels, each cooling channel being shaped to carry a cooling flow so as to exchange heat by convection with at least one elementary module,
• a cooling probe disposed in a channel of the plurality of cooling channels and configured to measure at least one cooling property selected from humidity, temperature and pressure,
• a cooling flow generator configured to generate the cooling flow to be conveyed in said channel or in another channel of the plurality of cooling
• control unit of said cooling flow generator configured to adjust, as a function of the measurement of the cooling property, at least one parameter of said cooling stream to be transported in said channel and / or said cooling stream to be transported in the other channel.
• the temperature of the oxidation units of each elementary module is regulated by means of a limited number of sensors, in particular by means of a single sensor.
• the at least one parameter of said cooling stream may be selected from temperature, pressure, flow rate, rate of cooling flow at the output of the cooling flow generator, and combinations thereof.
• the fuel cell may comprise a sensor disposed in an elementary module in fluid communication with the cathodic supply channel in which the cathodic power supply probe is arranged and / or able to exchange heat by convection with a flow. coolant flowing in the cooling channel in which the cooling probe is disposed, said sensor being configured to measure an electrical resistance selected from internal resistance, battery, polarization resistance of the cell, or total resistance of the cell. battery.
• the control unit of said cathode power supply generator is configured to adjust, as a function of the measurement of the cathodic power supply property and the measurement of the electrical resistance, at least one parameter of said supply flow.
• cathode to be carried in said channel and / or said cathode feed stream to be transported in the other channel, and / or the control unit of said cooling flow generator is configured to adjust according to the measurement of the property of cooling and measuring the electrical resistance, at least one parameter of said cooling flow to be transported in said cooling channel and / or said cooling flow to be transported in the other cooling channel.
• the fuel cell comprises at least one diaphragm and / or at least one flap configured to limit the input flow of the cathode supply channel and / or the cooling channel.
• a means for generating the cathode power supply and / or cooling flow may be the displacement of the flying object.
• all the shutters and / or diaphragms are controlled by a single control module flaps and / or diaphragms configured to arrange the flaps and / or diaphragm in the same open or closed configuration.
• the shutters and / or diaphragms may be arranged all facing a side face of the stack.
• the flaps and / or diaphragms disposed opposite the openings of the cooling channels may be arranged facing the same face as the flaps and / or diaphragms arranged opposite the openings of the cathode supply channels.
• flaps and / or diaphragms may be arranged on other lateral faces, and in particular on an opposite face.
• the battery may have a height of between 20 mm and 600 mm and / or a width of between 20 mm and 600 mm, and / or a depth of between 20 mm and 600 mm.
• the mass of the fuel cell may be between 0.01 kg and 10 kg.
• the fuel cell is configured to generate an electric power of between 1 W and 50 kW.
• the cell has a mass density of power of between 100 W.kg 1 and 5000 W.kg- 1 .
• the invention also relates to a method for manufacturing a fuel cell according to the invention, comprising a step of manufacturing at least one elementary module, preferably according to any one of the first and second aspects of the invention, the manufacturing step of the elementary module comprising the fixing, preferably bonding, an anode block, respectively a cathode block, on an oxidation unit.
• At least two, preferably at least ten elementary modules are manufactured, and the elementary modules are stacked on top of one another in a stacking direction.
• at least one adhesive composition is deposited on the anode block, respectively on the cathode block, and / or on the oxidation unit, and the anode block, respectively the cathode block, is then assembled with the unit of FIG. oxidation so as to form a fixing bridge rigidly fixed to the anode block, respectively to the cathode block, and to the oxidation unit.
• the adhesive composition can have a liquid or solid form.
• FIG. 6 schematically represents a fuel cell comprising a plurality of elementary modules according to the invention, seen in section along the stacking direction of the elementary modules,
• FIGS. 7 to 9 show diagrammatically in perspective variants of fuel cells according to the invention.
• FIG. 10 is a photograph of a battery according to one embodiment of the invention.
• the elementary module 5 of FIG. 1 extends along a longitudinal plane P having a longitudinal direction X. It comprises an oxidation unit 10 formed of a stack consisting in succession of an anode 15, of an electrolytic membrane 20 and a cathode 25, all three being each in the form of a plate extending in a plane parallel to the longitudinal plane.
• the electrolysis unit is disposed between an oxidant carrier 30 and a fuel carrier 35, each in the form of a porous plate extending in a plane parallel to the longitudinal plane of the elementary module.
• a cathode electron collector 40 in the form of a strip projecting in a transverse direction T in the longitudinal plane, is fixed on the oxidant carrier, thereby defining with the oxidant carrier a cathode block 45.
• cathode conductor bridge 50 formed of an electrically conductive adhesive.
• the cathode conductor bridge extends in the transverse direction between two opposite faces 55 and 60, one of them being in contact with the cathode electron collector, the other 60 being in contact with the cathode.
• the oxidizing carrier support, the cathodic electron collector, the cathodic conductor bridge and the cathode define a cathode chamber 65.
• the cathode feed stream for example generated by a fan and transported in a cathodic feed channel, as will be described later, passes through the porous oxidant carrier, as indicated by the arrow O to enter the cathode chamber and contact the cathode to ensure the oxidation reaction of the fuel.
• the cathodic electrons resulting from the oxidation reaction formed on the cathode can be collected and then, as indicated by the arrow Ec, can then be transferred via the cathodic collector bridge to the cathode electron collector.
• An anode electron collector 70 in the form of a protruding strip in the transverse direction, is attached to the fuel carrier 35, thereby defining with the fuel carrier a anode block 75.
• the collector Anode electrons are attached to the anode by means of an anodic conductor bridge 80 formed of an electrically conductive adhesive.
• the anode conductor bridge extends in the transverse direction between two opposite faces 85 and 90, one of them being in contact with the anode electron collector, the other 85 being in contact with the anode.
• the anode electrons resulting from the fuel oxidation reaction formed on the anode can be collected and then, as indicated by the arrow Ea, can then be transferred via the anodic conductor bridge to the collector of the anode. anodic electrons.
• the bonding fastenings of the anodic and cathodic blocks by means of the respective anodic and cathodic conductor bridges on the oxidation unit ensure the mechanical strength of the elementary module, without requiring the introduction of permanent compression means for this element. effect.
• an anodic sealing bridge 100 formed of an electrically insulating and fuel-tight adhesive seal, is sandwiched between the anode block and the fuel carrier and holds them at a distance from one of the another, defining an anode chamber 105 extending in a plane parallel to the longitudinal plane.
• the anodic sealing bridge forms a seal extending between the facing faces of the anode and the fuel carrier in a direction transverse to the longitudinal plane.
• the anodic sealing bridge surrounds said anode chamber in a plane parallel to the longitudinal plane. In addition to its sealing function described below, it strengthens the mechanical strength of the elementary module, adding additional fixation between the anode block and the oxidation unit. In operation, the fixing of the oxidation unit by means of the anodic sealing bridge and the anodic conducting bridge allows the elementary module to withstand the fuel pressure in the anode chamber, higher than the atmospheric pressure.
• the elementary module comprises a reservoir 108, defining an interior volume 1 10, comprising a filling orifice 1 15 for supplying the fuel tank.
• the fuel carrier support further defines a wall 1 18 separating the anode chamber from the interior volume of the tank.
• a compressor can inject a flow of fuel into the interior of the tank through the fill port, where the fuel is stored.
• the anode feed stream containing the fuel then passes through the fuel carrier carrier, which is porous and enters the anode chamber where it flows in a direction transverse to the longitudinal direction until contacting the anode , as indicated by arrow C.
• the anodic sealing bridge limits the flow of the fuel flow in the chamber in any direction contained in the longitudinal plane, as indicated by the arrows Li and L 2 , and thus reduces the leakage of fuel out of the anode chamber.
• the elementary module of FIG. 2 differs from the elementary module of FIG. 1 in that an anodic collector layer 120 and a cathodic collector layer 125 are disposed on the faces 130 and 135 of the anode and cathode respectively, arranged opposite the anode and cathode chambers respectively.
• the anodic and cathodic collector layers improve the collection of anode and cathode electrons generated remotely from the anode and cathode electron collectors, respectively.
• the electron-collecting layers may partially cover said anode and cathode faces, and for example be gas-tight to the fuel or to the oxidant, respectively.
• the fuel and the oxidant can come into contact with the anode and the cathode respectively in the zones of said faces of the anodes and cathodes not covered by the collector and cathode layers, respectively.
• the anodic and cathodic collection layers may also be in the form of a porous film with fuel and with the oxidant respectively, and cover for example integrally said faces of the anode and cathode respectively.
• the anodic conductor bridge 80 and the anodic sealing bridge 100 are fixed by bonding to the anode layer.
• the elementary module of Figure 2 comprises a cathodic fixing bridge 140 formed of an electrically insulating adhesive, extending between two opposite faces of the cathode chamber in a transverse direction in the longitudinal plane, one of the faces 145 of the cathodic fixing bridge being bonded to the oxidant carrier, the other side 150 of said bridge being bonded to the cathodic collector layer 125.
• the elementary module of FIG. 1 may include such a cathodic fixing bridge bonded to both the fuel carrier and the cathode.
• the elementary module of FIG. 3 differs from the elementary module of FIG. 2 in that the anode, respectively the cathode, comprises an anode window 155, respectively a cathode window 160, crossing the anode, respectively the cathode, in its thickness. , and flowing on the electrolyte membrane.
• the anodic conductor bridge 80 respectively the cathode conductor bridge 50, is housed in the anode window, respectively in the cathode window, and is fixed by bonding on the electrolytic membrane 10.
• the resistance strength of the elementary module is improved, the connections of the anode and cathode blocks respectively by means of the anodic and cathodic conductor bridges respectively with the oxidation unit being made directly with the electrolyte membrane.
• the anodic conductor bridge 80 respectively the cathodic conductor bridge 50 has a relief 165, 170 respectively protruding longitudinally and being disposed in contact with the anode collector layer, respectively of the cathodic collector layer.
• the relief of the anodic conducting bridge, respectively of the cathodic conductor bridge electrically contacts the anode, respectively the cathode with the anode electron collector, respectively with the cathode electron collector.
• FIG. 4 illustrates an embodiment of the fuel cell comprising a plurality of elementary modules 5 1 , 5 2 sharing the same electrolytic membrane 20.
• the fuel cell of FIG. 4 comprises elementary modules as illustrated in FIG. 3, which can obviously be combined and / or replaced by one or more elementary modules for example as illustrated in FIGS. 1 and 2.
• the elementary modules can share a same fuel carrier carrier and / or the same insulating carrier carrier. They can share or not share the same tank.
• FIG. 5 illustrates a fuel cell comprising an elementary module as illustrated in FIG. 2, further comprising a porous gas diffusion layer 170 superimposed on and in contact with the face of the oxidant carrier support opposite to the face next to the anodic chamber.
• the gas diffusion layer is disposed between the oxidant carrier and a porous grid 175 with which it is in contact.
• the fuel cell of FIG. 5 further comprises a first hollow tube 180, one wall of which is at least partially formed by the gate 175, which defines a cathode supply channel 185 for carrying a cathode feed stream. comprising the oxidant.
• the hollow tube comprises an inlet opening 190 for the cathode feed stream, as indicated by the arrow OE, arranged opposite a fan 200 capable of generating said cathode feed stream.
• the hollow tube furthermore has an outlet opening 205 through which the cathodic feed stream can escape, as indicated by the arrow Os after having passed through the porous grid 175 and the gas diffusion layer and fed, as indicated by the arrow O the cathode chamber 65 of the elementary module, and having loaded the products of the oxidation reaction.
• the oxidation reaction produces water vapor that is discharged from the anode chamber to the outlet opening through the flow of water.
• cathodic power supply in this case a flow of air.
• the fuel cell further has a second hollow tube 210 arranged so that the elementary module 5 is sandwiched between the first 185 and second 210 hollow tubes.
• the second hollow tube has a common wall with the reservoir. It defines a cooling channel 212 having an inlet opening 215 shaped for the inlet of a cooling stream R comprising a coolant such as air, disposed opposite a fan 220 configured to generate and distribute said cooling stream to said inlet opening.
• the elemental module When it flows in the cooling channel as indicated by the arrow R, the elemental module exchanges heat generated by the convection exothermic oxidation reaction at the wall 225 common to the module and the second hollow tube. The thus heated heating flow flows to an outlet opening 230 disposed opposite the inlet opening, through which it is removed from the fuel cell.
• the cathodic power supply and cooling channels extend in planes Pi and P 2 distinct and parallel to the longitudinal plane.
• the fan for generating the cooling flow and the fan for generating the cathodic feed stream comprising the oxidant are arranged opposite one and the same side face 235, parallel to the stacking direction DE, of the fuel cell.
• the fan to generate the flow cooling can be arranged on the side opposite to that opposite which the fan to generate the cathode feed stream is disposed.
• the battery can be free of means, such as for example described in FIG. 5, for cooling the battery by via a cooling flow.
• the fuel cell 250 of FIG. 6 comprises a plurality of four elementary modules 5a-d stacked one on the other in a stacking direction D E.
• Each elementary module of the plurality is identical to that illustrated in FIG. 5, except that the openings and outlets of the cooling channels are formed on faces perpendicular to those on which the openings and outlets of the cathode supply channels are formed. .
• the stacking direction D E is perpendicular to the longitudinal plane P of each elementary module.
• the fuel cell is shaped so that each pair of two consecutive elementary modules of the stack is such that said two elementary modules, for example 5a and 5b, are arranged head-to-tail with respect to each other according to the stacking direction.
• the modules of the stack are electrically connected by means of an electrical circuit, not shown, connecting an anode electron collector of an elementary module to a cathode electron collector of an adjacent elementary module.
• two consecutive elementary modules having facing cathode blocks are separated by channel 1 from a cathode power supply 255i_ 2 extending in a plane transverse to the stacking direction.
• a cathode power supply 255i_ 2 extending in a plane transverse to the stacking direction.
• two consecutive elementary modules whose anode blocks for example 75b and 75c, are disposed opposite and are separated by a cooling channel 260 extending in a plane transverse to the stacking direction.
• a cooling channel 260 extending in a plane transverse to the stacking direction.
• the two elementary modules 5b and 5c are cooled by convective exchange with the cooling flow R flowing in the channel.
• the fuel cell 250 of FIG. 6 is configured such that the cathode supply and cooling channels are spaced from each other and alternately in the stacking direction DE. In this way, the interactions between cathode feed stream O and cooling flow R are limited.
• the fuel cell of FIG. 6 includes two cathode power fans 200i_ 2 configured to each supply a respective cathode power channel 255i 2 with Associated cathode power stream and three 2201-3 cooling fans configured each to supply a cooling channel with associated cooling flows.
• the cathodic power fans and the cooling fans are arranged facing side faces 270, 275 of the stack perpendicular to each other. In this way, the cathode feed streams and the cooling streams flow in directions of flow respectively oblique to each other. The interaction between said streams is limited, which optimizes the energy efficiency of the battery.
• the fuel cell illustrated in FIG. 6 includes a cathode power supply probe 280 disposed in one of the cathode power supply channels for measuring the temperature of the cathodic power flow within said channel.
• the cathodic power supply probe is electrically connected to a control unit 285 of the anode supply fans of the battery, by means of connection that are not shown, said control unit being configured to adjust as a function of the temperature measurement by the cathodic power supply probe, for example the flow rate of the cathodic power supply flow at the output of each of the cathodic power supply fans of the fuel cell.
• the cathodic power flow rate of the plurality of cathode supply channels of the battery can be easily adjusted.
• the fuel cell of FIG. 6 further comprises a cooling probe 292 disposed in one of the cooling channels following the cathodic supply channel in which the cathodic power supply probe is arranged, for measuring the temperature of the cooling flow at the within the said channel cooling.
• the cooling probe is electrically connected to a control unit of the cooling fans 298 of the fuel cell, by means of connection not shown, said control unit being configured to adjust according to the measurement of the temperature by the probe cooling, for example the flow rate of the cooling stream at the outlet of each of the cooling fans of the fuel cell.
• the fuel cell further comprises a sensor 300 disposed within an elementary module for measuring, for example, the internal resistance of the elementary module.
• the sensor is connected to the control units of the cathode power supply and cooling fans which are each further configured to adjust the flow rates of the cathode power supply and cooling flow according to the internal resistance measurement of the elementary module.
• FIG. 7 schematically shows a fuel cell 250 comprising six elementary modules 5a-f stacked in a stacking direction DE, each elementary module being thin and extending along a longitudinal plane P normal to the stacking direction.
• the elementary modules of the fuel cell are arranged head to tail in pairs as in the example of FIG. 6.
• the fuel cell of FIG. 7 has the general shape of a right-hand block having four lateral faces 280a-d on which the inlets and outlets of the various cathodic power supply and cooling channels open.
• each cathodic power supply or cooling channel has an inlet opening 290a-c, respectively 295a-d opening on a side face opposite a cathode supply fan 300 respectively 305, and has outlet openings 310a-c, respectively 315a-d opening on each of the other three side faces of the stack.
• the cathode feed streams O on the one hand and the cooling streams R on the other hand flow in the respective channels in substantially perpendicular directions.
• each cathode supply channel and each cooling channel have openings on the four side faces 280a-d of the cell, the interactions with adverse consequences for the operation of the fuel cell, between cathode feed stream and cooling flows are limited.
• the fuel cell of FIG. 8 is an improved and preferred embodiment of the fuel cell of FIG. 7, wherein, for each cathodic supply channel, respectively cooling channel, the openings formed on the faces perpendicular to those on which the inlet opening of said channel is formed are closed by means of side walls.
• the flow of the cathodic feed stream, respectively the cooling flow is effected in the direction of the outlet opening 310, respectively 315 opening on the side face of the stack opposite to the side face on which opens out.
• the cathode feed streams and the cooling stream flow in perpendicular directions and at different heights in the stacking direction and do not interact.
• Such an arrangement favors the operation of the fuel cell over an extended operating temperature range.
• the inlet opening of the cathode feed stream can be closed so as to prevent the output of said flow, for example by means of masks referenced 320a-c between the dashed lines, for example polymer, in particular formed of foam .
• perpendicular to the lateral face on which the inlet opening of the cooling flow is formed can to be closed so as to prevent the output of said flow, for example by means of masks referenced 325a-c between the dashed lines, for example polymer, in particular formed of foam.
• the cathodic power and cooling streams flow in perpendicular directions and do not disturb.
• two consecutive elementary modules are arranged head to tail.
• two consecutive elementary modules can be arranged so that the anode block of the first elementary module is opposite the cathode block of the second elementary module.
• a solid separating plate extending in a longitudinal direction is arranged between the two consecutive elementary modules.
• the stack of FIG. 8 can be obtained by arranging two spacers between two consecutive elementary modules.
• the spacers are for example solid bars. They are spaced from each other so as to form the side walls of a cathode feed channel or a cooling channel.
• the fuel cell of FIG. 9 differs from the fuel cell of FIG. 8 in that each module has a length L that is at least two times greater than the width 1.
• each module has a length L that is at least two times greater than the width 1.
• several modules fans are arranged in the longitudinal direction X opposite the side face 280 on which open the openings 295a-d of the cooling channels.
• the 330i- 6 records indicate schematically the portion of the side face on which is directed the cooling flow.
• none of the elementary modules described in FIGS. 1 to 4 nor any of the fuel cells illustrated in FIGS. 5 to 9 comprise compression means for the plurality of elementary modules, such as clamping plates connected by tie rods of compression.
• a fuel cell a photograph of which is shown in FIG. 10, is formed by a stack of twelve elementary modules, each having a slender right-hand slab shape 117 mm long, 74 mm wide and thickness of 2 mm.
• This fuel cell is configured to oxidize dihydrogen as a fuel by the dioxygen of the air.
• Each elementary module weighs 8 g and is capable of generating an electrical power of 8 W.
• Two consecutive elementary modules are arranged head-to-tail in the stacking direction and are spaced apart by 1.2 mm, by means of a spacer formed of bars. foam whose opposite faces each in contact with one of said two consecutive modules, are covered with adhesive.
• the stack is in the form of a straight block, 117 mm long, 74 mm wide and 45 mm thick.
• the fuel cell has a volume of 0.4 liter and a mass of less than 150 g. It is capable of generating an electric power of 100W, and has a mass density of power of 0.67 Wg -1 . It is also suitable for generating electrical energy in a temperature range between -20 ° C and 50 ° C.
• the fuel cell has an internal resistance of 175 m ⁇ .cm 2 , similar to that of a battery of the prior art having terminal clamping plates and having a lower mass density of power for the same power generated. This internal resistance value indicates that the electron collection and the electrical connection of the elementary modules is of good quality.
• the pressure resistance measurements indicate that the fuel cell can support a maximum hydrogen pressure of 3 bar in the anode chamber of each elementary module.
• the leakage measurements by helium infiltration indicate that the leakage rate is low, less than 0.1 cm 3 / min.
• the performance of the present fuel cell can be compared to a fuel cell formed of a stack of modules compressed by terminal plates, marketed by Horizon FC.
• This battery operates in a temperature range lower between 0 ° C and 40 ° C and is able to generate a power of 200W.
• it has a mass of 470 g, and therefore a low power density equal to 0.42 Wg -1 compared to the fuel cell of the invention.
• the stack may comprise a compressor, a channel of distribution being connected to the compressor, the compressor being configured to deliver a cathode feed stream and / or a cooling stream to the input of the cathode supply channel and / or the cooling channel respectively.
• the cooling stream may comprise a heat transfer fluid other than air, for example a liquid, for example water or an oil.
• the fuel is not limited to dihydrogen. It may also be an alkane, for example selected from methane, propane, butane and mixtures thereof, or an alcohol in vapor form, for example selected from ethanol, methanol and mixtures thereof.
• the oxidant is not limited to oxygen. It can also be a gas comprising oxygen, for example air, or a mixture consisting of oxygen and nitrous oxide.

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• 2017
  • 2017-02-10 FR FR1751108A patent/FR3062958B1/fr active Active
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  • 2018-02-07 CN CN201880024386.6A patent/CN110537280B/zh active Active
  • 2018-02-07 EP EP18704945.7A patent/EP3580799A1/de active Pending
  • 2018-02-07 WO PCT/EP2018/053004 patent/WO2018146118A1/fr not_active Ceased
  • 2018-02-07 JP JP2019543245A patent/JP7025437B2/ja active Active

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