Classifications

• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M12/00—Hybrid cells; Manufacture thereof
  • H01M12/04—Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type
  • H01M12/06—Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type with one metallic and one gaseous electrode
  • H01M12/065—Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type with one metallic and one gaseous electrode with plate-like electrodes or stacks of plate-like electrodes
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M12/00—Hybrid cells; Manufacture thereof
  • H01M12/08—Hybrid cells; Manufacture thereof composed of a half-cell of a fuel-cell type and a half-cell of the secondary-cell type
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
  • H01M4/8605—Porous electrodes
  • H01M4/8615—Bifunctional electrodes for rechargeable cells
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
  • H01M4/88—Processes of manufacture
  • H01M4/8803—Supports for the deposition of the catalytic active composition
  • H01M4/8807—Gas diffusion layers
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
  • H01M4/88—Processes of manufacture
  • H01M4/8875—Methods for shaping the electrode into free-standing bodies, like sheets, films or grids, e.g. moulding, hot-pressing, casting without support, extrusion without support
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
  • H01M50/10—Primary casings; Jackets or wrappings
  • H01M50/138—Primary casings; Jackets or wrappings adapted for specific cells, e.g. electrochemical cells operating at high temperature
  • H01M50/1385—Hybrid 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
  • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
  • H01M8/023—Porous and characterised by the material
  • H01M8/0239—Organic resins; Organic polymers
• • 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
  • H01M8/18—Regenerative fuel cells, e.g. redox flow batteries or secondary fuel cells
  • H01M8/184—Regeneration by electrochemical means
• • 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
  • H01M8/22—Fuel cells in which the fuel is based on materials comprising carbon or oxygen or hydrogen and other elements; Fuel cells in which the fuel is based on materials comprising only elements other than carbon, oxygen or hydrogen
  • H01M8/225—Fuel cells in which the fuel is based on materials comprising particulate active material in the form of a suspension, a dispersion, a fluidised bed or a paste
• • 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
  • Y02E60/10—Energy storage using batteries
• • 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 application relates generally to the field of batteries and components of batteries. More specifically, the present application relates to the use of processes, materials, and structures/components to manage the interaction between the internal chemical reaction in a metal-air battery and the external environment. The concepts disclosed herein are further applicable to metal-air fuel cells.
• Metal-air batteries include a negative metal electrode (e.g., zinc, aluminum, magnesium, iron, lithium, etc.) and a positive electrode having a porous structure with catalytic properties for an oxygen reaction (typically referred to as the air electrode for the battery).
• An electrolyte is used to maintain high ionic conductivity between the two electrodes.
• the air electrode is usually made from thin, porous polymeric material (e.g.,
• a separator is provided between the anode and the cathode.
• Metal-air batteries provide significant energy capacity benefits.
• metal-air batteries have several times the energy storage density of lithium-ion batteries, while using globally abundant and low-cost metals (e.g., zinc) as the energy storage medium.
• the technology is relatively safe (non-flammable) and environmentally friendly (non-toxic and recyclable materials may be used). Since the technology uses materials and processes that are readily available in the U.S. and elsewhere, dependence on scarce resources such as oil may be reduced.
• a metal-air battery is a partially open system, in which the air electrode utilizes oxygen from the surrounding environment.
• One challenge associated with such an open system is that environmental conditions such as humidity and the presence of carbon dioxide (CO 2 ) may impact the battery, and in some cases may significantly shorten the lifespan of the battery. This in turn may limit the possible applications in which
• the electrode may flood.
• the humidity e.g., greater than 45 percent relative humidity
• moisture will be taken into the metal-air battery, causing a fall in electrolyte concentration and an increase in volume.
• the discharge performance of the metal-air battery will consequently be reduced and leakage of the electrolyte may occur.
• CO 2 may cause the pore structure of the air electrode to close up and that CO 2 may also cause a loss of conductivity (e.g., by displacing OH " (hydroxide) ions with CO 3 2" ).
• CO 2 may enter a metal-air battery from the external environment, it has also been suggested that CO 2 may be generated internally by the metal-air battery itself (e.g., through oxidation of the carbon support).
• peripheral systems e.g., fans, valves, humidifiers, CO 2 scrubbers, etc.
• Obvious shortcomings of such solutions include increased cost and complexity of the system, increased size (thus giving a lower effective energy density), and the fact that such solutions may not be suitable for use in certain applications (e.g., one would not want to use an external fan for a hearing aid battery).
• metal-air battery having a longer lifespan. It would also be advantageous to provide a metal-air battery that may be used in a variety of applications, including, but not limited to, large scale and small scale
• FIG. 1 is a perspective view of a metal-air battery in the form of a button cell according to an exemplary embodiment.
• FIG. 2 is a cross-sectional view of the metal-air battery shown in FIG. 1 taken along a line 2-2.
• FIG. 3 is a cross-sectional view of a metal-air battery similar to that shown in FIG. 1
• FIG. 4 is a cross-sectional view of a metal-air battery similar to that shown in FIG. 1.
• FIG. 5 is a cross-sectional view of a metal-air battery similar to that shown in FIG. 1.
• FIG. 6 is a perspective view of a metal-air battery in the form of a prismatic cell according to another exemplary embodiment.
• FIG. 7 is a cross-sectional view of the metal-air battery shown in FIG. 6 taken along line 7-7.
• FIG. 8 is a detail view of the cross-section of the metal-air battery shown in FIG. 7 taken along a line 8-8.
• FIG. 9 is a partially exploded perspective view of a flow battery according to an exemplary embodiment.
• FIGS. 10-18 are graphs illustrating the results from a number of experiments as described herein, and are intended to show the benefits of using an oxygen-selective material such as siloxane in a metal-air battery.
• a metal-air battery or cell that exhibits improved stability and performance when exposed to water vapor (e.g., the relative humidity) and other component elements of its surrounding environment (e.g., CO 2 ).
• the metal-air battery is configured to substantially retain water when the surrounding environment has low humidity, to resist flooding when the surrounding environment has high humidity, and to transition effectively between low and high humidity environments without substantially sacrificing these benefits.
• the metal-air battery is also configured to reduce undesirable effects that may result from exposure to CO 2 .
• one or more materials and structures/components may be incorporated into a metal-air battery to provide an improved lifespan without compromising high current density for the battery, enabling the battery to be used for a wide range of applications.
• the metal-air battery may have any desired configuration, including, but not limited to coin or button cells, prismatic cells, cylindrical cells, oval cells, flow cells, etc., or may have a fuel cell configuration. Further, the metal-air battery may be a primary
• a metal-air battery 10 shown in the form of a coin or button cell is illustrated according to an exemplary embodiment.
• the battery 10 includes a metal electrode 12, an air electrode 14, an oxygen-selective membrane in the form of a siloxane membrane 16 (hereinafter referred to as the "siloxane membrane"), an electrolyte 18, a separator 20, and an enclosing structure shown as a housing 22 according to an exemplary embodiment.
• the battery 10 is a zinc-air battery.
• the battery 10 may use other metals in place of the zinc, including, but not limited to, aluminum, magnesium, iron, lithium, cadmium, and/or a metal hydride.
• metal hydride materials include the AB 5 or AB 2 structure types where the "AB x " designation refers to the ratio of A elements and B elements.
• A may be a combination of La, Ce, Pr and Nd
• A may be Ti, Zr or a combination of Ti and Zr.
• B may be a combination of Ni, Mn, Co, Al and Fe.
• the housing 22 e.g., case, container, casing, etc.
• the housing 22 is shown as including a base 23 and a lid 24 according to an exemplary embodiment.
• a seal
• the lid 24 (e.g., a molded nylon sealing gasket, etc.) is formed or disposed generally between the base 23 (e.g., can, etc.) and the lid 24 (e.g., cap, cover, top, etc.) to help maintain the relative positions of the base 23 and the lid 24.
• the seal 25 also helps prevent undesirable contacts (e.g., causing a short circuit) and/or leakage.
• the lid 24 includes one or more holes
• the metal electrode 12 is shown disposed within the housing 22 at or proximate to the second portion 28.
• the air electrode 14 is shown disposed at or proximate to the first portion 27, and is spaced a distance from the metal electrode 12.
• the holes 26 provide for interaction between the air electrode 14 and the oxygen in the surrounding atmosphere (e.g., air).
• the surrounding atmosphere may be ambient air or one or more air flows may be directed into or across the holes 26.
• the housing may have any number of shapes and/or configurations according to other exemplary embodiments.
• the separator 20 is a thin, porous, film or membrane (e.g., a plastic film, an ion selective membrane, etc.) disposed substantially between the metal electrode 12 and the air electrode 14 according to an exemplary embodiment.
• the separator 20 is configured to prevent the short circuiting of the battery 10 by providing electrical isolation between the metal electrode 12 and the air electrode 14.
• the separator 20 includes or is made of polypropylene or polyethylene that has been treated to develop hydrophilic pores that are configured to fill with the electrolyte 18.
• the separator may be made of any material that is suited for preventing short circuiting of the battery 10 and/or that includes hydrophilic pores.
• the electrolyte 18 is shown disposed substantially between the metal electrode 12 and the air electrode 14 according to an exemplary embodiment.
• the electrolyte 18 e.g., potassium hydroxide (“KOH") or other hydroxyl ion-conducting media
• KOH potassium hydroxide
• OH hydroxyl ions
• the electrolyte 18 is disposed within some of the pores of the metal electrode 12 and some of the pores of the air electrode 14.
• the electrolyte may be partially absorbed into the air electrode to provide for a three-phase zone with a high surface area for the air electrode catalyst(s).
• the electrolyte may further be evenly distributed within the metal electrode, helping prevent uneven current distribution in the metal electric load as the reaction moves from the surface of the zinc electrode
• the distribution and location of the electrolyte may vary.
• the composition of the electrolyte may help prevent and or manage CO 2 production within the cell.
• the electrolyte 18 is an alkaline electrolyte used to maintain high ionic conductivity between the metal electrode and the air electrode.
• the electrolyte may be any electrolyte that has high ionic conductivity and/or high reaction rates for the oxygen reduction/evolution and the metal oxidation/reduction reactions (e.g., NaOH, LiOH, KOH, etc.).
• the electrolyte may include salt water or others salt- based solutions that give sufficient conductivity for the targeted applications (e.g., for marine/military applications, etc.).
• the electrolyte may be organic-based, water-based, or a combination of organic-based and water-based.
• the metal electrode and the electrolyte are combined (e.g., mixed, stirred, etc.).
• the combination of the metal electrode and the electrolyte may form a paste, powder, pellets, slurry, etc.
• the air electrode 14 includes one or more layers with different properties and a current collector (e.g., a metal mesh, which also helps to stabilize the air electrode).
• a current collector e.g., a metal mesh, which also helps to stabilize the air electrode.
• a plurality of air electrodes may be used for a single battery.
• at least two of the air electrodes have different layering schemes and/or compositions.
• the current collector is other than a metal mesh current collector (e.g., a foam current collector).
• the air electrode 14 includes a gas diffusion layer 30 (sometimes abbreviated "GDL”) and an active layer 32 (sometimes abbreviated "AL”) according to an exemplary embodiment.
• GDL gas diffusion layer 30
• A active layer 32
• the gas diffusion layer 30 is shown disposed proximate to the holes 26 in the second portion 28 of the housing 22, substantially between the active layer 32 and the gas diffusion layer 30.
• the gas diffusion layer 30 includes a plurality of pores 33 according to an exemplary embodiment.
• the gas diffusion layer 30 is configured to be porous and hydrophobic, allowing gas to flow through the pores while acting as a barrier to prevent liquid flow.
• both the oxygen reduction and evolution reactions take place in one or more air electrode layers closely bonded to this layer.
• the active layer 32 is disposed substantially between the metal electrode 12 and the holes 26 in the second portion 28 of the housing 22 according to an exemplary embodiment.
• the active layer 32 has a double pore structure that includes both
• hydrophobic pores 34 and hydrophilic pores 36 The hydrophobic pores help achieve high rates of oxygen diffusion, while the hydrophilic pores 36 allow for sufficient electrolyte penetration into the reaction zone for the oxygen reaction (e.g., by capillary forces).
• the hydrophilic pores may be disposed in a layer separate from the active layer, e.g., an oxygen evolution layer (sometimes abbreviated "OEL").
• OEL oxygen evolution layer
• other layers or materials may be included in/on or coupled to the air electrode.
• gas selective materials may be included in the pore structure.
• the air electrode 14 may include a combination of pore forming materials.
• the hydrophilic pores of the air electrode are configured to provide a support material for a catalyst or a combination of catalysts (e.g., by helping anchor the catalyst to the reaction site material) (e.g., cobalt on carbon, silver on carbon, etc.).
• the pore forming material includes activated carbon or graphite (e.g., having a BET surface area of more than 100 m ⁇ g "1 ).
• pore forming materials such as high surface area ceramics or other materials may be used.
• support materials or pore forming materials that are not carbon-based avoids CO 2 formation by those support materials when charging at high voltages (e.g., greater than 2V).
• high voltages e.g., greater than 2V.
• the silver can be Raney Ag, where the high surface area is obtained by leaching out alloying element from a silver alloy (e.g., Ag-Zn alloy).
• any material that is stable in alkaline solutions, that is conductive, and that can form a pore structure configured to allow for electrolyte and oxygen penetration, may be used as the pore forming material for the air electrode.
• the air electrode internal structures may be used to manage humidity and CO 2 .
• a current collector 39 is disposed between the gas diffusion layer 30 and the active layer 32 of the air electrode 14 according to an exemplary embodiment.
• the placement of the current collector 39 facilitates assembly of the siloxane membrane 16 and the air electrode 14.
• the current collector may be disposed on the active layer (e.g., when a non-conductive layer or no gas diffusion layer is included in the air electrode).
• the current collector 39 may be formed of any suitable electrically-conductive material.
• the air electrode 14 further includes a binding agent or combination of binding agents 40, a catalyst or a combination of catalysts 42, and/or other additives (e.g., ceramic materials, high surface area metals or alloys stable in alkaline media, etc.).
• the binding agents 40 are included in both the active layer 32 and the gas diffusion layer 30, and the catalysts 42 are included in the active layer.
• the binding agents, catalysts, and/or other additives may be included in any, none, or all of the layers of the air electrode.
• the air electrode may not contain one or more of a binding agent or combinations of binding agents, a catalyst or a combination of catalysts, and/or other additives.
• the binding agents 40 are intended to provide increased mechanical strength for the air electrode 14, while providing for maintenance of relatively high diffusion rates of oxygen (e.g., comparable to more traditional air electrodes that typically use
• the binding agents 40 may also cause pores in the air electrode 14 to become hydrophobic.
• the binders include PTFE in combination with other binders. According to other exemplary embodiment
• thermoplastics such as polybutylene terephthalate or polyamides, polyvinylidene fluoride, silicone-based elastomers such as polydimethylsiloxane, or rubber materials such as ethylene propylene, and/or combinations thereof.
• silicone-based elastomers such as polydimethylsiloxane
• rubber materials such as ethylene propylene, and/or combinations thereof.
• the binding agents 40 provide mechanical strength sufficient to allow the air electrode 14 to be formed in a number of manners, including, but not limited to, one or a combination of extrusion, stamping, pressing, utilizing hot plates, calendering, etc.
• This improved mechanical strength also enables air electrode 14 to be formed into any of a variety of shapes (e.g., a tubular shape, etc.).
• the ability to form the air electrode into any of a variety of shapes may assist in the manufacture of metal-air batteries for applications such as Bluetooth headsets, applications for which tubular batteries are used or required (e.g., size AA batteries, size AAA batteries, size D batteries), etc.
• the catalysts 42 are configured to improve the reaction rate of the oxygen reaction.
• catalytically active metals or oxygen- containing metal salts are used (e.g., Pt, Pd, Ag, Co, Fe, MnO 2 , KMnO 4 , MnSO 4 , SnO 2 , Fe 2 O 3 , CoO, C ⁇ 3 ⁇ 4 , etc.).
• a combination of more than one catalytically active material may be used.
• the battery 10 is a secondary battery (e.g., rechargeable) and the air electrode 14 is a bifunctional air electrode.
• additional catalysts or catalyst combinations capable of evolving oxygen may be used in addition to the catalysts and/or combinations of catalysts described above.
• catalysts may include, but are not limited to, WC, TiC, CoWO 4 , FeWO 4 , NiS, WS 2 , La 2 O 3 , Ag 2 O, Ag, spinels (i.e., a group of oxides of general formula AB 2 O 4 , where A represents a divalent metal ion such as magnesium, iron, nickel, manganese and/or zinc and B represents trivalent metal ions such as aluminum, iron, chromium and/or manganese) and perovskites (i.e., a group of oxides of general formula AXO 3 , where A is a divalent metal ion such as cerium, calcium, sodium, strontium, lead and/or various rare earth metals, and X is a tetrahedral metal ion such as titanium, niobium and/or iron where all members of this group have the same basic structure with the XO 3 atoms forming a framework of interconnected octahedron
• the air electrode 14 is formed in a three- step process.
• Each layer of the multi-layer air electrode 14 is formed separately.
• the desired component elements of each layer are mixed together.
• the pore forming materials, the catalysts, the binding materials and/or other additives are mixed under the influence of mechanical, thermal, or mechanical and thermal energy. In this process it is desirable that the materials be well distributed. If the mixture contains a hydrophobic binding agent, then this binding agent forms a three dimensional network connecting the powders into an agglomerate.
• the mixture or the agglomerate is then typically extruded and/or calendered into a layer.
• one or more layers typically having differing properties (e.g., the gas diffusion layer and the active layer), are combined using heat and/or pressure (e.g., by calendering and/or pressing).
• the current collector is pressed or calendered into the combined layers (e.g., into the active layer, into the gas diffusion layer, between the active layer and the gas diffusion layer, etc.).
• the air electrode may be formed using other processes.
• a dry mixing process is utilized in the first step to form the layers of air electrode 14.
• a dry mixing process all of the ingredients of a layer are mixed together in the form of dry powders.
• a dry process utilizes PTFE binders having a particle size below 1 mm as a binder and an additional pore forming aid such as ammonium bicarbonate to create the gas diffusion layer and/or the oxygen evolution layer.
• a wet mixing process may instead be utilized. In a wet mixing process, one or more solvents are added at the beginning or during the mixing process, or, alternatively, one or more ingredients may be used in the form of a dispersion or suspension.
• a wet process utilizes PTFE that is suspended in water as a binder and a pore forming aid such as ammonium bicarbonate to create the oxygen evolution layer.
• the various individual layers may be made using different methods.
• some of the layers may be produced using a dry mixing process, while others may be produced using a wet process.
• it is possible to combine both dry and wet processes for the different layers and the production may be performed in a continuous production line according to PCT publication WO 2005/004260, the disclosure of which is hereby incorporated by reference.
• An oxygen evolution layer may be included in the air electrode.
• the oxygen evolution layer may includes 2 to 15 percent binding agent by weight and 25 to 65 percent catalyst(s) by weight.
• the remainder of the oxygen evolution layer may include a high surface area carbon and/or graphite material and possibly some other additives.
• the active layer is prepared using a mixture of 15 percent PTFE by weight (e.g., in powder form with a particle size below 1 mm from Lawrence Industries of Thomasville, NC as a binding agent), 70 percent high surface area carbon (e.g., XC 500 from Cabot) by weight as a pore forming agent, and 15 percent manganese sulfate (e.g., MnSO 4 from Prolabo of France) by weight as a catalyst.
• 15 percent PTFE by weight e.g., in powder form with a particle size below 1 mm from Lawrence Industries of Thomasville, NC as a binding agent
• 70 percent high surface area carbon e.g., XC 500 from Cabot
• 15 percent manganese sulfate e.g., MnSO 4 from Prolabo of France
• the binding agent, the pore forming agent, and the catalyst are mixed together (e.g., in a single-shaft rotary mixer at approximately 1,000 rpm) to form a substantially homogeneous mixture.
• the mixture is heated to a desired temperature.
• the powder is milled to form an agglomerate.
• the mixture may be heated to a desired temperature at or near 90 0 C and milled at approximately 1,000 rpm for 1 hour, or the mixture may be heated to a lower initial temperature, but milled at a higher rpm (e.g., 10,000 rpm).
• the agglomerate is pressed into a brick (e.g., a brick of about 2 mm thickness) and then calendered into a sheet (e.g., of about 0.5 mm thickness).
• a brick e.g., a brick of about 2 mm thickness
• a sheet e.g., of about 0.5 mm thickness
• the temperatures, milling rates and times, and other parameters may vary depending on the particular materials used and other factors.
• the gas diffusion layer is formed using a mixture of 25 percent PTFE by weight (e.g., in powder form with a particle size below 1 mm from Lawrence Industries of
• the binding agent and the pore forming agent are mixed at a desired temperature (e.g., typically below a maximum temperature of 40 0 C) in a single-shaft rotary mixer (e.g., for 2 hours at 1,500 rpm) to form an agglomerate.
• the agglomerate is pressed into a brick (e.g., of about 2 mm thickness) and then calendered into a sheet (e.g., of about 1 mm thickness).
• the active layer is prepared using 15 percent PTFE by weight in a suspension containing 60 percent PTFE by weight dispersed in water (e.g., from Sigma-Aldrich, Inc.) as a binding agent, 65 percent high surface area carbon (e.g., XC 500 from Cabot) by weight as a pore forming agent, and 20 percent manganese sulfate (e.g., MnSO 4 from Prolabo of France) by weight as catalysts.
• the high surface area carbon is mixed with both catalysts in water.
• the PTFE suspension is mixed with water.
• the PTFE suspension is then added to the carbon suspension and mixed to form a slurry agglomerate.
• the slurry is then mixed (e.g., in an ultrasonic bath for 30 minutes) and subsequently dried (e.g., at 300° C for 3 hours) to remove any surfactants.
• the dried mixture is then agglomerated and a hydrogen treated naphtha with a low boiling point (e.g., Shellsol D40 from Shell Chemicals of London) is added to form a paste. Finally, the paste is calendered into a thin layer to form the active layer.
• a hydrogen treated naphtha with a low boiling point e.g., Shellsol D40 from Shell Chemicals of London
• the hydrophobic gas diffusion layer may be formed by the same method according to an exemplary embodiment. In this layer only high surface area carbon (65 percent by weight) and PTFE (35 percent by weight) are used. The final layer is relatively thin (e.g., having a thickness of about 0.8 mm).
• the active layer and the gas diffusion layer are then coupled (e.g., by calendering) to form the air electrode (e.g., having a total thickness of 0.8 mm).
• a current collector e.g., nickel mesh
• the air electrode may then be dried (e.g., at 70 0 C for 8 hours) to create the hydrophobic porosity of the gas diffusion layer and to remove the ammonium bicarbonate therefrom.
• the layers may be formed to have a variety of thickness and/or compositions. Further, the layers may be coupled by any of a number of methods known in the art.
• a membrane shown as a siloxane membrane 16 is disposed adjacent to the air electrode 14 (i.e., located substantially adjacent to the gas diffusion layer 30 of the air electrode 14 between the gas diffusion layer 30 and the holes 26 in the housing 22).
• the siloxane membrane is 16 is a selective membrane that allow gases such as oxygen to pass through the membrane while acting as a moisture barrier to prevent moisture from entering and exiting the battery. This in turn helps to maintain the water balance within the battery 10.
• the siloxane membrane 16 is configured to improve the performance and usable lifetime of the battery 10 by preventing or slowing down the drying out of the electrolyte and the flooding of the air electrode.
• the siloxane membrane 16 is configured to prevent water from the electrolyte 18 from leaving the battery 10 (e.g., when the relative humidity less than 45 percent relative humidity or some other relative humidity that would result in water loss), thus helping to avoid the loss in the power density and efficiency of the battery that occurs when electrolyte dries out.
• the siloxane membrane 16 is also configured to prevent flooding of the battery 10 (e.g., when the relative humidity is greater than 45 percent or some other relative humidity that would result in flooding), helping to prevent the electrolyte 18 from leaking therefrom (when the electrolyte leaks from the battery, the electrolyte concentration (the ratio between electrolyte and Zn) falls, resulting in significant decreases in the discharge performance and the ability to store metal-air batteries long-term.
• the siloxane membrane 16 helps stabilize, improve the performance of, and prolong the lifetime of the battery 10, significantly expanding the potential commercial uses of metal-air batteries.
• the siloxane membrane 16 is also configured to prevent ingress of CO 2 through the holes 26 in the housing. It is known that CO 2 consumes OH " ions in electrolyte, increases the evaporation of water, and forms non-hygroscopic crystals. By preventing CO 2 from entering the housing 22, the siloxane membrane 16 helps preserve the electrolyte 18 and maintain the water balance within the battery 10.
• the siloxane membrane 16 has a thickness of between approximately 0.1 ⁇ m and 200 ⁇ m (although the thickness may be greater according to other exemplary embodiments, for example, the thickness of the membrane may be between 1 and 50 ⁇ m, less than or equal to 10 ⁇ m, less than or equal to 6 ⁇ m, less than or equal to 3 ⁇ m, or any other suitable thickness as may be appropriate under the circumstances), and has suitable mechanical strength to allow its production using a wide range of manufacturing methods.
• the greater the thickness of the siloxane membrane the better it will be expected to perform in preventing CO 2 and water vapor from being transported into and/or out of battery 10 (e.g., because of the longer diffusion path).
• the thickness of siloxane membrane 16 may be varied depending on the intended application for the battery, since the thickness of an applied membrane/film is expected to be directly proportional to the current density that can be achieved for a battery. For example, for applications using a relatively low current density (e.g., lower power applications such as batteries for watches, sensors, RFID tags, etc.), films with relatively greater thicknesses may be used (e.g., a 100 ⁇ m film that provides a maximum current density of 2 mA/cm ).
• siloxane film of lesser thickness e.g., a 3 ⁇ m film that can provide a maximum current density of more than 50 mA/cm 2 at above 1 V.
• the thickness of the selective membrane may be tailored to achieve a desired current density. This will be described in more detail below with respect to FIG. 17. According to other exemplary embodiments, any selective membrane material having a thickness/diffusion coefficient combination sufficient to both stabilize a metal-air battery while maintaining a desired performance level may be utilized.
• increasing the surface area of the air electrode may allow for the use of thicker siloxane films that still allow the battery to achieve a desired current density.
• a larger surface area allows for a higher reaction rate, since the current density (mA/cm 2 ) is determined by the thickness of the siloxane film, while the current (mA) is determined by the current density and the surface area of the air electrode available for the application.
• the siloxane membrane 16 also allows for the use of larger and/or more holes 26 in the housing 22 for oxygen access than would otherwise be possible (e.g., more air may be allowed to enter the battery when the siloxane membrane 16 is used because of its beneficial protections against dry out and flooding). This allows the battery 10 to operate at higher currents without oxygen diffusion limitations and increased dry out rates.
• a primary coin cell e.g., size 675 zinc-air battery may show diffusion limitation at about 30 mA due to the limited oxygen access. Providing a hole of more than 5 mm in diameter gives a pulse current of more than 100 mA without diffusion limitations.
• housing 22 e.g., casing, containers, etc.
• the current density of the battery is not limited by the access of oxygen through the holes, but, rather, by the transport of oxygen through the selective membrane.
• the selective membranes having high transport properties for oxygen, this also opens the possibility to use metal-air batteries for higher power applications (e.g., laptops, cars, etc.).
• the siloxane membrane 16 does not include a support layer (e.g., a finely porous film, a non-woven fabric, etc.), because the thickness of the siloxane membrane 16 itself provides sufficient stability and structural integrity for the given application. This also provides for improved handling during manufacture of the batteries and resistance against the formation of pin holes. For thinner siloxane membranes (e.g., membranes having a thickness below approximately 20 ⁇ m), there may be some advantage to using a support layer.
• a support layer e.g., a finely porous film, a non-woven fabric, etc.
• the improved mechanical strength of the siloxane membrane also provides for a wide range of formation and application methods.
• the siloxane membrane formation process may include stamping, pressing, and/or other processes or combinations of processes that would not be able to be utilized or be utilized as well with thinner and/or weaker films or membranes, as will be discussed in more detail below. Further, the improved formation and applications methods enable the battery 10 to be used in a wider range of applications.
• the siloxane membrane 16 is formed using siloxane Geniomer® 80 from Wacker Chemie AG of Kunststoff, Germany.
• Geniomer® 80 is a reaction product of silicone resin with silicone fluids, which forms water-repellent release films. These films have much better affinity than is attainable with
• the oxygen diffusion coefficient for a 10 ⁇ m thick film is approximately 6.2E- 11 m /s.
• other siloxane materials may be used (e.g., siloxane from Folex Imaging, Celfa AG, CM Celfa Membranes, etc.).
• the oxygen diffusion coefficient for a 20 ⁇ m thick film made with the siloxane from Celfa is approximately 5.7E-11 m /s.
• the siloxane membrane may be made conductive for use on top of the gas diffusion layer.
• materials e.g., in the form of particles may be added to the siloxane membrane to enable the siloxane membrane to function as the current collector for the battery cathode.
• Exemplary materials include, but are not limited to, carbon (e.g., graphite) particles and metallic particles.
• a siloxane membrane may be made conductive by dip coating the gas diffusion layer into a siloxane solution. A siloxane film is then created within the pore structure of the gas diffusion layer at the same time as the conductive support material (carbon) allows for electronic contact with the current collector.
• the siloxane membrane may be positioned outside of the housing instead of within the housing as shown in FIG. 2.
• FIG. 3 illustrates an exemplary embodiment of a metal-air battery 110 including a siloxane membrane 116 positioned outside of the housing 122.
• the siloxane membrane 116 is shown disposed on a porous support film 144 and positioned substantially over the holes 126 that are included in the housing 122. This configuration may be particularly desirable, for example, if the battery 110 is placed in a housing that has a larger surface area than the battery case.
• a porous support material e.g., made of a polymer such as PTFE
• siloxane which may fill in some of the pores of the support material
• a porous support material including a siloxane additive may be positioned over the holes.
• the siloxane membrane may be integrated with the housing.
• a battery having a housing in the form of a soft pouch could incorporate siloxane into the pouch material.
• siloxane into the pouch material.
• the siloxane membrane may be provided proximate to or within the air electrode.
• the siloxane membrane may take the place of or act as the gas diffusion layer.
• FIG. 4 illustrates another exemplary embodiment of a metal-air flow battery 210 including an air electrode 214 and a siloxane membrane 216.
• the air electrode 214 includes an active layer 232 without an associated gas diffusion layer.
• the siloxane layer 216 is shown as being disposed adjacent to the active layer 232.
• This configuration provides a number of advantages, including, but not limited to, providing enhanced long lifetime stability and safety against leakage because the siloxane layer 216 is substantially a solid membrane that will not allow liquid penetration and is also selective to oxygen to prevent CO 2 from entering the cell.
• siloxane may be mixed with the materials of the gas diffusion layer to form a single conductive siloxane membrane layer.
• FIG. 5 illustrates another exemplary embodiment of a metal-air flow battery 310 that includes a siloxane material 316 and an air electrode 314.
• the air electrode 314 is shown including an active layer 332 and a gas diffusion layer 330.
• the siloxane material 316 is included in the gas diffusion layer 330.
• the siloxane material is mixed with the other gas diffusion layer materials and then formed into the gas diffusion layer.
• multiple metal electrodes and air electrodes may be provided in a single metal-air battery.
• siloxane membrane and the air electrode are discussed independently for the purposes of this disclosure, it should be recognized that the siloxane membrane may be considered to be a layer of the air electrode.
• the siloxane membrane 16 may be used in combination with additional layers (e.g., one or more layers of porous plastic materials, one or more metal layers, etc.) to achieve a desired selectivity for oxygen, water vapor management, and carbon-dioxide management for battery 10.
• additional layers e.g., one or more layers of porous plastic materials, one or more metal layers, etc.
• the selectivity for O 2 transport while preventing water vapor and CO 2 passage may be improved. Since the rate of transport of oxygen is slow through silver, this additional layer needs to be very thin and will therefore require a support material for deposition.
• Siloxane can act as this support material, and also advantageously has high oxygen transport properties.
• the ability to precisely control the siloxane membrane thickness the ability to ensure that the siloxane membrane is substantially pinhole free, the ability to handle the siloxane membrane in mass manufacturing without damaging it, and the ability to assemble the siloxane membrane and the metal-air battery.
• the siloxane membrane 16 from Wacker is co-extruded with a low density polyethylene (LDPE) transfer layer into a two-layer co-extruded film (e.g., membrane, sheet, etc.).
• the siloxane membrane is a 10 ⁇ m Geniomer® 80 film at least partially covering (e.g., disposed on top of, etc.) a 60 ⁇ m LDPE film, making the total thickness of the co-extruded film 70 ⁇ m.
• siloxane membranes having a wide range of thicknesses can be obtained by this method (e.g., a combined thickness of less than 50 ⁇ m, a combined thickness of more than 50 ⁇ m, etc.).
• the co-extrusion process helps to ensure an even thickness of the siloxane membrane and/or the other extruded layers.
• the co-extrusion process also allows one or more of these layers to be relatively easily delaminated, so that the siloxane membrane layer is removable and can be assembled to the air electrode.
• the film is subsequently checked for homogeneity and to ensure that relatively few to no pores are present therein (e.g., by measuring the air permeability).
• Process parameters such as temperature, pressure, thickness, extrusion speed, and feed screw type may be controlled to help ensure the homogeneity of the siloxane membrane and to help ensure that relatively few to no pores are present in the siloxane membrane.
• the co-extruded film is placed onto the gas diffusion layer side of the air electrode, so that the siloxane membrane 16 is facing the air electrode 14.
• a rand (e.g., 5 mm) for the glue used in the assembly of battery 10 is left uncoated by siloxane membrane 16.
• the air electrode 14 and the co-extruded siloxane membrane are then calendered to adhere to one another (e.g., between 2 silicon papers and 2 cellulose papers in a 2-step calendering process two step to a combined thickness of 1.62 cm).
• the upper LDPE transfer layer is then removed, leaving the air electrode with the siloxane membrane at least partially covering its gas diffusion layer side.
• the siloxane membrane is co-extruded onto a backing or transfer layer (e.g., plastics such as LDPE, etc.).
• the transfer layer provides for improved handling of the siloxane membrane and reduces the risk of pinholes and cracks in the siloxane membrane during assembly with the air electrode.
• the co-extruded layer including both the siloxane membrane and the transfer layer is placed onto the air electrode with the siloxane membrane facing the gas diffusion layer.
• the co-extruded siloxane membrane and the air electrode are then adhered to one another using a lamination and/or calendering process.
• the transfer layer can be removed relatively easily as the adhesive forces between the air electrode and the siloxane membrane are strong.
• the siloxane membrane and the air electrode may be coupled/adhered to one another by any number of processes utilizing heat and/or pressure.
• the siloxane membrane is co-extruded onto a transfer layer.
• One or more layers of the air electrode e.g., the active layer, the gas diffusion layer, all layers of the air electrode, etc.
• a lamination and/or calendering process may be used to reduce the thickness. While multi-layer co- extrusion processes have been described above, the extrusion process may be a single layer extrusion process. Further, the multi-layer co-extrusion processes may include more than two co-extruded component layers, materials, etc.
• the siloxane membrane is deposited onto a transfer layer.
• the deposition process may include, but is not limited to, casting (solvent or aqueous), spraying (solvent or aqueous), contact printing (e.g., screen stencil, flexography, gravure, off-set, etc.), non-contact printing (e.g., inkjet), spin-coating, and chemical vapor deposition.
• This deposition process may then be followed by a process utilizing heat and/or pressure (e.g., laminating, calendering, etc.) to remove pinholes, flatten the structure, and/or achieve a desired thickness of the siloxane membrane.
• the siloxane membrane, once deposited on the transfer membrane may then be coupled or adhered to the air electrode (e.g., by a calendering and/or lamination process).
• the siloxane membrane is deposited directly onto the air electrode.
• the deposition process may include, but is not limited to, casting (solvent or aqueous), spraying (solvent or aqueous), contact printing (e.g., screen stencil, flexography, gravure, off-set, etc.), non-contact printing (e.g., inkjet), spin-coating, and chemical vapor deposition.
• This deposition process may then be followed by a process utilizing heat and/or pressure (e.g., laminating, calendering, etc.) to remove pinholes, flatten the structure, and/or achieve a desired thickness of the siloxane membrane and/or the air electrode.
• the siloxane membrane is coupled or adhered to the housing of the metal-air battery.
• the siloxane membrane may be coupled or adhered to the interior or the exterior of the case.
• the siloxane membrane may or may not be further adhered to the air electrode.
• a process involving heat and/or pressure e.g., laminating, calendering, etc.
• a deposition process may be used to adhere the siloxane membrane to the housing.
• the deposition process may include, but is not limited to, casting (solvent or aqueous), spraying (solvent or aqueous), contact printing (e.g., screen stencil, flexography, gravure, off-set, etc.), non-contact printing (e.g., inkjet), spin-coating, and chemical vapor deposition.
• an overmolding process may be used.
• the siloxane membrane may be overmolded by a material (e.g., a porous material) that forms the housing.
• a material e.g., a porous material
• other variations on an overmolding process may be used.
• any process sufficient to couple or adhere the siloxane membrane (or a selective membrane of a material or materials other than siloxane) to the air electrode and/or the housing of the metal-air battery may be used. None of these processes require the use of a support layer. Further, at one or more times during any of these exemplary processes, a process utilizing heat and/or pressure may be included to remove pinholes, flatten the structure, achieve a desired thickness of the siloxane membrane and/or the air electrode, and/or to achieve other desired characteristics for the siloxane membrane and/or the air electrode.
• a heat/radiation source e.g., ultraviolet radiation source, an infrared radiation source, etc.
• a heat/radiation source e.g., ultraviolet radiation source, an infrared radiation source, etc.
• a heat source e.g., a ultraviolet radiation source
• the siloxane membrane and air electrode are then washed to remove non- patterned (cured) areas.
• siloxane membranes may be utilized in conjunction with batteries of other configurations as well (e.g., prismatic cells, cylindrical cells, oval cells, flow cells, fuels cells, etc.).
• the placement of the siloxane membrane in batteries of different configurations may be similar to that used for coin cells (e.g., placed between the cell housing and the air electrode, coupled to the exterior surface of the housing, or other configurations or placements as described herein, etc.).
• FIGS. 6-8 a prismatic metal-air (e.g., zinc-air) battery 410 is shown according to an exemplary embodiment.
• FIG. 7 shows a cross-sectional view of the battery 410
• FIG. 8 shows a detail view of one end of the battery 410 taken across line 8-8 in FIG. 7.
• the battery 410 includes a housing 422, a metal electrode 412 running along the length of the cell, an air electrode 414, and an electrolyte 418 provided in the space between the metal electrode 412 and the air electrode 414.
• the electrolyte 418 also resides inside the pores of the metal electrode 412 and partly inside the pores of the air electrode 414.
• a siloxane membrane 416 (similar to that described with respect to the siloxane membrane 16 for the coin cell embodiment described above) is provided on top of/adjacent to the air electrode 414.
• the siloxane membrane 416 has a thickness greater than 0.1 ⁇ m and provides for improved humidity and CO 2 management for the battery, while still providing for a desired rate of oxygen diffusion.
• the upper portion of the housing 422 contains holes 426 (e.g., slots, apertures, etc.) for air to enter the battery 410.
• the air electrode 414 and siloxane membrane 416 may be secured (e.g., by gluing) to the lid of the housing to prevent leakage.
• the gas diffusion layer side of the air electrode faces the holes 426 in the battery housing 422, and the siloxane membrane 416 is positioned substantially between the gas diffusion layer and the holes 426 in the housing 422.
• the battery 410 is filled with a metal (e.g., zinc) paste.
• Current collectors for the air electrode and the metal electrode may be attached using contact pins by resistance welding, laser welding, or other methods known in the art and shielded (e.g., with glue) to prevent gassing in the cell.
• the housing is then closed off (other than the air holes) (e.g., by ultrasonic welding).
• the battery 410 provides for a commercially viable prismatic battery that may be used in numerous applications wherein prismatic batteries are or may be used because battery 410 provides, in addition to a high current density, a lifetime in that is sufficient and/or desirable for these applications (e.g., cell phones, cameras, MP3 players, portable electronic devices, etc.).
• Siloxane membranes may also be used in flow batteries such as those described in International Application PCT/US 10/40445 and corresponding U.S. Patent Application No. 12/826,383, filed June 29, 2010, each filed June 29, 2010, the entire disclosures of which are incorporated herein by reference.
• FIG. 9 illustrates an exemplary embodiment of a flow battery 510.
• a metal-air flow battery shown as a zinc-air flow battery 510 including a siloxane membrane 516 is shown according to an exemplary embodiment.
• the term "flow battery” is intended to refer to a battery system in which reactants are transported into and out of the battery. For a metal-air flow battery system, this implies that the metal anode material and the electrolyte are introduced (e.g., pumped) into the battery and a metal oxide is removed from or taken out of the battery system. Like a fuel cell, the flow battery system requires a flow of reactants through the system during use.
• the zinc-air flow battery 510 is shown as a closed loop system including a zinc electrode 512, an electrolyte 518, one or more storage devices shown as tank or chamber 544, and a reactor 546 having one or more reaction tubes 548, each including an air electrode 514.
• the zinc electrode 512 is combined with the electrolyte 518 to form a zinc paste 550, which serves as a reactant for the zinc-air flow battery 510, according to an exemplary embodiment.
• the reactant e.g., active material, etc.
• the reactant is configured to be transported (e.g., fed, pumped, pushed, forced, etc.) into and out of the reactor 546.
• the zinc paste 550 is transported into the reactor 546 and through the reaction tubes 548 and a zinc oxide paste 552 is transported out of the reactor 546 after the zinc paste 550 reacts with the hydroxyl ions produced when the air electrode 514 reacts with oxygen from the air.
• the zinc oxide paste 552 is transported into the reactor 546 and through the reaction tubes 548 and the zinc paste 550 is transported out of the reactor 546 after the hydroxyl ions are converted back to oxygen.
• the pastes 550, 552 are stored in the tank 544 before and after being transported through the reactor 546, the zinc paste 550 being stored in a first cavity 554 of the tank 544 and the zinc oxide paste 552 being stored in a second cavity 556 of the tank 544.
• the reaction tubes 546 each include an air electrode 514 disposed between at least two protective layers.
• FIG. 9 illustrates one of the reaction tubes 548 of the zinc-air flow battery 510 in more detail, exploded from the zinc-air flow battery 510 according to an exemplary embodiment.
• the reaction tube 548 is shown having a layered configuration that includes an inner tube or base 558, a separator 560, the air electrode 514, and an outer tube or protective casing 562 according to an exemplary embodiment.
• the base 558 is shown as the innermost layer of the reaction tube 546
• the protective casing 562 is shown as the outmost layer of the reaction tube 546
• the other layers are shown disposed substantially between and concentric with the base 558 and the protective casing 562.
• the composition of air electrodes 514 enables production of tubular air electrodes according to an exemplary embodiment.
• the air electrode 514 includes a plurality of binders 564.
• the binders 564 provide for increased mechanical strength of the air electrode 514, while providing for maintenance of relatively high diffusion rates of oxygen (e.g., comparable to more traditional air electrodes).
• the binders 564 may provide sufficient mechanical strength to enable the air electrode 514 to be formed in a number of manners, including, but not limited to, one or a combination of extrusion, stamping, pressing, utilizing hot plates, calendaring, etc. This improved mechanical strength may also enable air electrode 514 to be formed into any of a variety of shapes (e.g., tubular, etc.).
• the tubular configuration of the reaction tubes 546, and, correspondingly, the air electrodes 514, makes the air electrodes 514 relatively easy to assembly without leakage.
• the tubular configuration in conjunction with the conductive gas diffusion layer permits for the current collectors for the air electrodes 514 to be on the outside of the reaction tubes 546, substantially preventing any leakage from the air electrode current collector. Further, the tubular configuration permits for the current collectors for zinc electrodes 512 to be integrated substantially within reaction tubes 546, eliminating contact pin leakage.
• the tubular configuration of air electrodes a 514 provides improved resistance to pressure, erosion (e.g., during transport of zinc paste 550 and zinc oxide paste 552, etc.), and flooding.
• the tubular configuration of the air electrode permits zinc paste to flow through a passage 560 defined thereby with less friction than if the air electrode were configured as a flat plate, causing relatively less erosion therewithin.
• the cylindrical reaction tubes 546 having a layered configuration permits for incorporation of elements/layers providing mechanical stability and helping to provide improved pressure resistance.
• the siloxane membrane 516 is shown disposed to the exterior of a gas diffusion layer 530 and an active layer 532 of the air electrode 514 in the reaction tube 546 according to an exemplary embodiment.
• the siloxane membrane 516 By including the siloxane membrane 516 in the zinc-air flow battery 510, less electrolyte 518 is needed in the tank 522 to accommodate the water loss attendant with its operation (e.g., as a result of vaporization, etc.). Further, by reducing the negative effects of CO 2 on the zinc-air flow battery 510, the siloxane membrane 516 reduces the need for peripherals and maintenance (e.g., CO 2 scrubbers, etc.). According to other exemplary embodiments, the air electrode and the siloxane membrane may be otherwise configured.
• the siloxane membrane may replace the gas diffusion layer or be positioned exterior to the protective casing 562.
• siloxane may be incorporated into the reaction tube other than in the form of a membrane.
• siloxane material may be incorporated into one or more layers of the air electrode.
• the siloxane membrane 516 of the metal- air flow battery 510 may be extruded to be tubular and then calendered onto the gas diffusion layer 530 of the air electrode 514.
• the siloxane membrane may be extruded into a flat sheet that is disposed or wrapped about the air electrode and then adhered (e.g., by laminating or calendering) thereto.
• the siloxane membrane may be formed and adhered or coupled to the air electrode and/or housing of a flow cell via any one or combination of the processes described above with reference to the siloxane membrane 516.
• the zinc paste 550 is fed from the first cavity 554 through a zinc inlet/outlet and distributed amongst the reaction tubes 546 by a feed system 572.
• the feed system 572 includes a plurality of
• the screws 574 rotate in a first direction, transporting the zinc paste 550 from proximate the first end portion 576 toward the second end portion 578 of each reaction tube 546.
• An air flow 580 is directed by an air flow system 582, shown including fans 584, through a plurality of air flow channels 586 defined between the reaction tubes 546.
• the air flow 580 is at least partially received in the reaction tubes 546 through a plurality of openings 588 in the protective casing 562 and toward the passage 566, as shown by a plurality of air flow paths 590.
• Oxygen from the air flow 580 is converted to hydroxyl ions in the air electrode 514; this reaction generally involves a reduction of oxygen and consumption of electrons to produce the hydroxyl ions.
• the hydroxyl ions then migrate toward the zinc electrode 512 in the zinc paste 550 within the passages 566 of the reaction tubes 546.
• the hydroxyl ions cause the zinc to oxidize, liberating electrons and providing power.
• the zinc paste 550 is converted to the zinc oxide paste 552 within the reaction tubes 546 and releases electrons.
• the zinc oxide paste 552 continues to be transported toward the second end portion 578.
• the zinc oxide paste 552 is eventually transported from reaction tubes 546 through a zinc oxide inlet/outlet and deposited in the second cavity 556 of the tank 544.
• the zinc-air flow battery 510 is rechargeable.
• the zinc oxide paste 552 is converted or regenerated back to zinc paste 550.
• the zinc oxide paste 552 is fed from the second cavity 556 and distributed amongst the reaction tubes 546 by the feed system 572.
• the screws 574 rotate in the second direction (i.e., opposite to the direction they rotate during discharging), transporting the zinc oxide paste 552 from proximate the second end portion 578 toward the first end portion 576 of each reaction tube 546.
• the zinc oxide paste 552 is reduced to form the zinc paste 550 as electrons are consumed and stored.
• Hydroxyl ions are converted to oxygen in the air electrodes 514, adding oxygen to the air flow 580. This oxygen flows from the reaction tubes 546 through the openings 588 in the protective casing 562 outward from proximate the passage 566, as shown by the air flow paths 590.
• metal-air batteries that do not utilize a siloxane membrane are limited by environmental conditions (e.g., the presence of CO 2 , humidity, etc.), which limit the battery life and performance (e.g., standby lifetime).
• Metal-air coin or button cells are currently the only metal-air batteries that are commercially available/utilized in a large volumes. Most commonly, these metal-air batteries are used in hearing aids. These batteries have a relatively long shelf life due to closed air access packaging, but dry out within relatively quickly (e.g., approximately within five weeks of removing the tape covering the holes in the housing of the metal-air coin cell) because, when in use, the surrounding environmental conditions cause a slow capacity loss of the metal-air coin cell batteries.
• siloxane membrane e.g., siloxane membrane 16, and/or siloxane additives (e.g., in the gas diffusion layer or active layer of the air electrode).
• FIGS. 10-13 are graphs illustrating the effect that CO 2 has on the tendency for an electrolyte to dry out, and illustrate the percentage weight change for an electrolyte over time.
• KOH potassium hydroxide
• FIGS. 10 and 11 illustrate the effects of CO 2 absorption on the percentage weight change of a KOH electrolyte over time in an environment having approximately 35 percent relative humidity.
• Various KOH/water solutions (7.7M, 10.2M, and 12.8M) were provided in a watchglass in a CO 2 -free environment (FIG. 3) and in a CO 2 -containing environment, and the percentage weight change of the electrolyte over time was monitored. As can be seen in FIG.
• FIGS. 12 and 13 illustrate substantially the same behavior as shown in FIGS. 10 and 11, with the difference being that the results shown in FIGS. 12 and 13 were obtained using prismatic cell prototypes having an air electrode but no metal electrode (instead of using a watchglass as in FIGS. 10 and 11).
• Test cells were prepared using various types of air electrodes, with the concentration of the KOH electrolyte being 7.7 M. Again, the KOH solutions in the CO 2 -containing environment tended to dry out over time, as evidenced by the downward sloping lines indicative of continued weight loss in the electrolyte as shown in the FIG. 13 graph.
• FIG. 14 and 15 are graphs illustrating the results of an experiment intended to examine the effects of CO 2 on the concentration of hydroxides in a prismatic prototype metal-air battery over time. The results indicate that the hydroxide concentration is reduced by the presence of CO 2 . In the CO 2 -free environment, FIG. 14 shows that the
• FIG. 15 shows a dramatic reduction in hydroxide concentration with time.
• the concentration of K 2 C ⁇ 3 remains relatively constant at a very low value, while in the presence of CO 2 , the K 2 C ⁇ 3 increases with increasing time.
• Hydroxide concentration also affects the capacity of the metal-air battery anode. With decreasing hydroxide concentration, the capacity of the battery tends to decrease. Accordingly, CO 2 can both dry out the metal-air battery and decrease the capacity of a metal-air battery by decreasing the concentration of hydroxides in the metal-air battery. This again illustrates the importance of preventing CO 2 from entering the battery.
• metal-air e.g., zinc-air
• KOH is hygroscopic and K 2 CO 3 has low hygroscopic properties
• KOH is converted to K 2 CO 3 in the presence of CO 2
• the stability of the battery is compromised (e.g., it dries out, shortening its lifespan).
• FIG. 16 is a graph illustrating the benefit that a siloxane membrane may have to mitigate against the adverse effects of CO 2 described above.
• Prismatic metal-air battery prototypes (not including metal electrodes) were prepared, with some of the prototypes including a 50 ⁇ m thick siloxane membrane (using siloxane from Celfa) disposed on a gas diffusion layer of an air electrode (the other prototypes were prepared without the siloxane membranes, and are denoted as "blanks" in the data).
• a 9 M KOH electrolyte solution was used for the cells.
• the sample sells were monitored over time while being exposed to CO 2 at a relative humidity of 35%, and a temperature of 25°C.
• the prismatic prototype metal-air batteries that included the siloxane membrane experienced only a slight reduction in hydroxide concentration after more than 800 hours, while those prototypes that did not include a siloxane membrane exhibited a drop in the hydroxide concentration to less than IM during the same time frame (during which time the concentration of K 2 CO 3 increased).
• slowing CO 2 intake to a metal-air battery helps keep the hydroxide concentration stable and reduces the tendency to form K2CO3. Accordingly, the significant improvement in the hydroxide concentration with the use of the siloxane membrane illustrated in the results shown in FIG.
• FIG. 17 illustrates data examining the relationship between siloxane membrane thickness and the oxygen diffusion limit for test cells.
• Prototype metal-air batteries were manufactured which incorporated siloxane membranes of various thicknesses (3, 6, and 10 microns) and the current density was monitored during discharged and compared to prototype batteries that did not utilize a siloxane membrane. All experiments were performed in a half cell setup with a 7 M KOH electrolyte at 25 0 C. The exposed air electrode surface was 3 cm 2 .
• the siloxane films were placed onto a porous polypropylene support material in a separate layer and placed on top of the gas diffusion layer facing the air side. The siloxane films were co-extruded with a support material as described above, and the support material was removed as the siloxane films were transported onto the porous support material, as described above.
• the air electrode may be coated with a siloxane solution (either by dipping a prepared air electrode into a siloxane solution or by applying a siloxane solution to the exterior of all or a portion of the air electrode using other means) to impregnate the air electrode with siloxane.
• an air electrode was coated with a siloxane material using a dipping process. Following preparation of the air electrode, the electrode was immersed in a siloxane solution (e.g., 5.8% siloxane in isopropanol) for a relatively short period of time (in this case, approximately one second, although coating times may differ according to other exemplary embodiments) to coat the air electrode.
• a siloxane solution e.g., 5.8% siloxane in isopropanol
• the air electrode was then placed in a vacuum chamber for approximately ten minutes to remove any air entrapped in the air electrode structure and to force the siloxane into the pores of the air electrode. After the vacuum treatment, excess solution was removed from the air electrode using a paper towel (according to other exemplary embodiments, air drying or other suitable methods may be employed). The air electrode was then dried in an oven (e.g., at 7O 0 C for a period of 15 hours, although the temperature and time may differ according to other exemplary embodiments). During the oven drying step, the gas diffusion layer was positioned facing upward, and a thin film will be visible on the gas diffusion layer after drying is complete.
• an oven e.g., at 7O 0 C for a period of 15 hours, although the temperature and time may differ according to other exemplary embodiments.
• a non-treated air electrode i.e., one that was not coated with a siloxane solution
• the blank was prepared in the same batch as the siloxane-treated air electrode.
• the experiment was repeated several times. It was surprisingly discovered that the initial charge and discharge profile was superior for the air electrodes that were dip coated in a siloxane solution as compared to the air electrodes that were not dip coated in a siloxane solution. This is illustrated, for example, in FIG. 18, which shows initial charge and discharge curves at 20 mA/cm for cells having 6 M KOH electrolytes that incorporate either the treated or untreated air electrodes.
• the voltage during charge and discharge took time to normalize (e.g., approximately 120 hours), as illustrated, for example, by the fact that the charging portion of the curve was above the 2.0 volt level and gradually decreased with each charge cycle until it normalized around 2.0 volts.
• the treated air electrodes grey lines
• the treated air electrodes cycled around a voltage range consistently throughout the testing, and did not require time to normalize to the 2.0 volt level.
• Battery formation operations are typically performed to ensure that the battery exhibits regular and predictable charge and discharge cycling. If such battery formation operations were not performed with untreated air electrodes, it would be more difficult to create accurate battery charging/discharging algorithms, since the response of the battery would be unknown until the battery normalized.
• a siloxane solution to coat all or a portion of the air electrode, the battery formation process may be eliminated, which in turn may reduce the time and cost of manufacturing air electrodes and metal-air batteries (e.g., if the need to perform an initial set of charge/discharge cycles is eliminated, lengthy initial charge and discharge operations can be eliminated from the manufacturing process, saving both time and resources).
• the siloxane solution was applied only onto the gas diffusion side of a first air electrode and onto the active layer side of another air electrode (e.g., by brushing the solution onto the respective layers).
• the sample with siloxane on the gas diffusion side did not show any significant difference from the untreated sample relating to the electrochemical performance during charge and discharge.
• the sample treated on the active layer side of the air electrode showed similar performance improvements as for the air electrode fully immersed into the siloxane solution.
• siloxane applied in a dipping process also has the advantageous benefit of improving the activation of the air electrode. This differs from the conventional wisdom relating to battery formation, where it was believed that activation of the battery required a slow wet up of the active layer during an extended battery formation charge/discharge cycling process.
• the term “coupled” means the joining of two members directly or indirectly to one another. Such joining may be stationary or moveable in nature. Such joining may be achieved with the two members or the two members and any additional intermediate members being integrally formed as a single unitary body with one another or with the two members or the two members and any additional intermediate members being attached to one another. Such joining may be permanent in nature or may be removable or releasable in nature.

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