WO2010111567A1 - Improved cathode - Google Patents

Improved cathode Download PDF

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Publication number
WO2010111567A1
WO2010111567A1 PCT/US2010/028772 US2010028772W WO2010111567A1 WO 2010111567 A1 WO2010111567 A1 WO 2010111567A1 US 2010028772 W US2010028772 W US 2010028772W WO 2010111567 A1 WO2010111567 A1 WO 2010111567A1
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WO
WIPO (PCT)
Prior art keywords
cathode
dopant
cell
powder
silver
Prior art date
Application number
PCT/US2010/028772
Other languages
French (fr)
Inventor
George W. Adamson
Hieu M. Duong
Ximei Sun
Original Assignee
Zpower, Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Zpower, Inc. filed Critical Zpower, Inc.
Priority to EP10756896.6A priority Critical patent/EP2411563B1/en
Priority to CA2757062A priority patent/CA2757062C/en
Priority to AU2010229828A priority patent/AU2010229828B2/en
Priority to US13/259,315 priority patent/US20120164526A1/en
Priority to JP2012502275A priority patent/JP5638058B2/en
Publication of WO2010111567A1 publication Critical patent/WO2010111567A1/en
Priority to US14/230,020 priority patent/US9209454B2/en

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    • 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
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/362—Composites
    • H01M4/364—Composites as mixtures
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/24—Alkaline accumulators
    • H01M10/32—Silver accumulators
    • 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
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/24—Electrodes for alkaline accumulators
    • H01M4/34—Silver oxide or hydroxide electrodes
    • 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
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/621—Binders
    • H01M4/622—Binders being polymers
    • H01M4/623—Binders being polymers fluorinated polymers
    • 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

Definitions

  • This invention is concerned with a new cathode formed by doping a cathode material with a dopant that imparts the cathode with one or more improved properties over traditional cathodes.
  • the anode When a traditional battery is discharged, the anode supplies positive ions to an electrolyte and electrons to an external circuit.
  • the cathode is typically an electronically conducting host into which positive ions are inserted reversibly from the electrolyte as a guest species and are charge-compensated by electrons from the external circuit.
  • a secondary battery, or cell uses a reaction that can be reversed when current is applied to the battery, thus '"recharging" the battery.
  • the chemical reactions at the anode and cathode of a secondary battery must be reversible.
  • Electrode materials such as cathode active materials suffer a number of drawbacks. For instance, many traditional cathodes possess art elevated impedance or internal resistance that negatively effects battery discharge, and thus, restricts battery performance. As many traditional batteries progress through charge cycles, the deleterious effect of impedance causes an increased hindrance on battery performance. [0005] Thus, there is a need for electrode materials that have improved properties and can improve battery performance.
  • One aspect of the present invention provides a cathode for use in an electrochemical cell comprising a silver material that is doped with a trivalent dopant to give a doped silver material, wherein the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the cathode.
  • the cathode further comprises from about 0.5 wt% to about S wt% of bivalent dopant
  • the cathode further comprises from about 1 wt% to about 8 wt% of trivalent dopant.
  • the doped silver material comprises a powder.
  • the doped silver material comprises a powder, and the powder has a mean particle diameter of about 20 ⁇ m or less.
  • the doped silver material comprises a powder, and the powder has a mean particle diameter of about IS ⁇ m or less. Ih other examples, the powder has a mean particle diameter of about 5 ⁇ m or less.
  • the silver material comprises Ag, AgO, Ag 2 O, Ag 2 O 3 , AgOH, AgOOH, AgONa, AgCuO 2 , AgFeO 2 , AgMnO 2 , Ag(OH) 2 , or any combination thereof.
  • Some cathodes of this aspect further comprise a binder.
  • the cathode further comprises a binder, and the binder comprises FTFE or PVDF.
  • the dopant comprises at least one Group 13 element.
  • the dopant comprises aluminum, indium, gallium, boron, thallium, or any combination thereof, hi other examples, the dopant comprises aluminum, indium, gallium, boron, or any combination thereof, hi some embodiments, the dopant comprises a lanthanide element.
  • the lanthanide element is Yb.
  • Another aspect of the present invention provides a cathode for use in an electrochemical cell comprising a doped silver material comprising a dopant, wherein the dopant comprises gallium, boron, or a combination thereof, and the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the cathode, hi some embodiments of this aspect, the cathode comprises from about 0.5 wt% to about 5 wt% of dopant In some embodiments of this aspect, the cathode comprises from about 1 wt% to about 8 wt% of dopant In other embodiments, the doped silver material of the cathode comprises a powder.
  • the doped silver material comprises a powder, and the powder has a mean particle diameter of about 20 ⁇ m or less.
  • the doped silver material comprises a powder, and the powder has a mean particle diameter of about 15 ⁇ m or less, hi another example, the powder has a mean particle diameter of about 5 ⁇ m or less, hi some embodiments of this aspect, the silver material comprises Ag, AgO, Ag 2 O, Ag 2 O 3 , AgOH, AgOOH, AgONa, AgCuO 2 , AgFeO 2 , AgMnO 2 , Ag(OH) 2 , or any combination thereof.
  • Other cathodes of this aspect further comprise a binder.
  • the cathode further comprises a binder, and the binder comprises PTFE or PVDF.
  • the dopant comprises gallium.
  • the dopant comprises boron.
  • the dopant comprises a lanthanide element.
  • the lanthanide element is Yb.
  • the cathode further comprises from about 0.S wt% to about S wt% of dopant. In some embodiments of this aspect, the cathode further comprises from about 1 wt% to about S wt% of dopant.
  • the doped silver material comprises a powder.
  • the doped silver material comprises a powder, and the powder has a mean particle diameter of about 20 urn or less. In other examples, the doped silver material comprises a powder, and the powder has a mean particle diameter of about 15 ⁇ m or less. In another example, the powder has a mean particle diameter of about 5 ⁇ m or less.
  • the doped silver material comprises Ag, AgO, Ag 2 O, Ag 2 O 3 , AgOH, AgOOH, AgONa, AgCuO 2 , AgFeO 2 , AgMnO 2 , Ag(OH) 2 , or any combination thereof .
  • Some cathodes of this aspect further comprise a binder.
  • the cathode further comprises a binder, and the binder comprises PTFE or PVDF.
  • the dopant comprises indium. In others, the dopant comprises aluminum.
  • Another aspect of the present invention provides a method of producing a cathode for use in an electrochemical cell comprising providing a silver powder that is doped with from about 0.25 wt% to about 10 wt% of a trivalent dopant by weight of the cathode to give a doped silver powder; and forming the doped silver powder into a cathode.
  • the doped silver powder is doped with from about 0.5 wt% to about 5 wt% of dopant In some methods, the doped silver powder is doped with from about 1 wt% to about 8 wt% of dopant In other methods, the doped silver powder has a mean particle diameter of about 20 ⁇ m or less, hi some methods, the doped silver powder has a mean particle diameter of about 15 ⁇ m or less. For example, the doped silver powder has a mean particle diameter of about 5 ⁇ m or less.
  • the doped silver powder comprises Ag, AgO, Ag 2 O, Ag 2 O 3 , AgOH, AgOOH, AgONa, AgCuO 2 , AgFeO 2 , AgMnO 2 , Ag(OH) 2 , or any combination thereof.
  • the doped silver powder comprises AgO, Ag 2 O, Ag 2 O 3 , or any combination thereof.
  • Some methods further comprise the step of providing a binder.
  • the method further comprises providing a binder, wherein the binder comprises PTFE or PVDF.
  • the dopant comprises a lanthanide.
  • the dopant comprises Yb.
  • the dopant comprises at least one Group 13 element.
  • the dopant comprises gallium, boron, indium, aluminum, thallium, or any combination thereof.
  • the dopant comprises gallium, boron, or a combination thereof.
  • the dopant comprises indium, aluminum, or a combination thereof.
  • Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein the dopant comprises a trivalent dopant, and the dopant is present in a sufficient concentration to impart the cell with at least 70% (e.g., at least 80%, at least 85%, or at least 90%) capacity over at least 100 cycles (e.g., at least 150 cycles, at least 120 cycles, at least 200 cycles, at least 250 cycles, at least 300 cycles, at least 320 cycles, at least 350 cycles, or at least 400),
  • the present invention provides an electrochemical cell comprising a cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein the dopant comprises a trivalent dopant, and the dopant is present in a sufficient concentration to impart the cell with about 80% or greater (e.g., at least 85%, at least 85%, or at least
  • the present invention provides an electrochemical cell comprising & cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein the dopant comprises a trivalent dopant, and the dopant is present in a sufficient concentration to impart the cell with about 80% or greater (e.g., at least 85%, at least 85%, or at least 90%) capacity over at least 150 cycles.
  • the silver material comprises from about 0.25 wt% to about 10 wt% of trivalent dopant.
  • the silver material comprises from about 0.5 wt% to about 5wt% of trivalent dopant.
  • the silver material comprises a powder.
  • the silver material comprises a powder, and the powder has a mean particle diameter of about 20 ⁇ m or less, In other examples, the silver material comprises a powder, and the powder has a mean particle diameter of about 15 ⁇ m or less. In other examples, the powder has a mean particle diameter of about 5 ⁇ m or less.
  • the cathode, the anode, or both further comprises a binder, In some embodiments, the cathode further comprises a binder. For instance, the cathode comprises a binder, and the binder comprises PTFE or PVDF. In other embodiments, the anode further comprises a binder. For instance, the anode further comprises a binder, and the binder comprises PTFE or PVDF.
  • the silver powder comprises Ag, AgO, Ag 2 O, Ag 2 O 3 , AgOH, AgOOH, AgONa, AgCuO 2 , AgFeO 2 , AgMnO 2 , Ag(OH) 2 , or any combination thereof.
  • the silver powder comprises AgO, Ag 2 O, Ag 2 O 3 , or any combination thereof.
  • the silver material comprises AgO.
  • the dopant comprises at least one Group 13 element.
  • the dopant comprises indium, aluminum, gallium, boron, thallium, or any combination thereof.
  • the dopant comprises indium, aluminum, or a combination thereof. And in some examples, the dopant comprises gallium, boron, or a combination thereof. In some embodiments, the dopant comprises a lanthanide element.
  • the lanthanide element is Yb.
  • an electrochemical cell comprising a cathode comprising silver powder comprising from about 0.25 wt% to about 10 wt% of a trivalent dopant; an anode comprising zinc; and an electrolyte comprising KOH.
  • the silver powder has a mean particle diameter of about IS ⁇ m or less. Ih other examples, the powder has a mean particle diameter of about S ⁇ m or less.
  • the cathode, the anode, or both comprise a binder.
  • the cathode comprises a binder.
  • the cathode comprises a binder, and the binder comprises PTFE or FVDF.
  • the anode comprises a binder.
  • the anode comprises a binder, and the binder comprises PTFE or PVDF.
  • Other embodiments further comprise an electrolyte comprising NaOH, KOH, or a combination thereof.
  • the silver powder comprises Ag, AgO, Ag 2 O, Ag 2 Oa, AgOH, AgOOH, AgONa, AgCuO 2 , AgFeO 2 , AgMnO 2 , Ag(OH) 2 , or any combination thereof.
  • the silver powder comprises AgO, Ag 2 O, Ag 2 Os, or any combination thereof.
  • the silver material comprises AgO.
  • the silver material comprises Ag 2 O.
  • the dopant comprises at least one Group 13 element.
  • the dopant comprises indium, aluminum, gallium, boron, thallium, or any combination thereof.
  • the dopant comprises indium, aluminum, or a combination thereof.
  • the dopant comprises gallium, boron, or a combination thereof.
  • Another aspect of the present invention provides a cathode for use in an electrochemical cell comprising a doped silver material comprising a dopant, wherein the dopant comprises a lanthanide element, aluminum, indium, gallium, boron, or a combination thereof, and the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the doped silver material.
  • the lanthanide element comprises Yb.
  • FIGURE 1 is an exploded view of an exemplary electrochemical cell of the present invention that was employed in cell cycle testing described in Example Nos. 4 and 7;
  • FIGURE 2 is a graphical plot of charge-discharge testing for an exemplary electrochemical cell of the present invention, which is superimposed on a graphical representation of charge-discharge testing results for a control electrochemical test cell; and
  • FIGURE 3 is a graphical plot of the actual capacity of an exemplary cell of the present invention as a function of cycle number.
  • the present invention provides cathodes, methods of making cathodes, and electrochemical cells (e.g., batteries) that employ these cathodes having improved properties over traditional cathodes, methods, or electrochemical cells.
  • electrochemical cells e.g., batteries
  • the term “battery” encompasses electrical storage devices comprising one electrochemical cell or a plurality of electrochemical cells.
  • a “secondary battery” is rechargeable, whereas a “primary battery” is not rechargeable.
  • a battery anode is designated as the positive electrode during discharge, and as the negative electrode during charge.
  • the terms “silver material” or “silver powder” refer to any silver compound such as Ag, AgO, Ag 2 O, Ag 2 O 3 , AgOH, AgOOH, AgONa, AgCuO 2 , AgFeO 2 , AgMnO 2 , Ag(OH) 2 , hydrates thereof, or any combination thereof.
  • hydrates' of silver include hydroxides of silver. Because it is believed that the coordination sphere surrounding a silver atom is dynamic during charging and discharging of the cell wherein the silver serves as a cathode, or when the oxidation state of the silver atom is in a state of flux, it is intended that the term 'silver* or 'silver material' encompass any of these silver oxides and hydrates (e.g., hydroxides). Terms 'silver' or 'silver material 1 also includes any of the abovementioned species that are doped and/or coated with dopants and/or coatings that enhance one or more properties of the silver. Exemplary dopants and coatings are provided below.
  • silver or silver material includes a silver oxide further comprising an indium or aluminum dopant or coating, m some examples, silver or silver material includes a silver oxide further comprising Group 13 elements. In some examples, silver or silver material includes a silver oxide further comprising a bivalent dopant.
  • oxide used herein does not, in each instance, describe the number of oxygen atoms present in the silver or silver material.
  • a silver oxide may have a chemical formula of AgO, Ag 2 Os, or a combination thereof.
  • silver can comprise a bulk material or silver can comprise a powder having any suitable mean particle diameter.
  • iron oxide refers to any oxide or hydroxide of iron, e.g., FeO, Fe 2 O 3 , Fe 3 O 4 , or any combination thereof.
  • boron oxide refers to any oxide or hydroxide of boron, e.g., B 2 O 3 .
  • aluminum oxide refers to any oxide or hydroxide of aluminum, e.g., Al 2 O 3 .
  • gallium oxide refers to any oxide or hydroxide of gallium, e.g., Ga 2 O 3 .
  • indium oxide refers to any oxide or hydroxide of indium, e.g., In 2 O 3 .
  • thalium oxide refers to any oxide or hydroxide of thalium, e.g., Th 2 O 3 .
  • Group 13 elements refers to one or more of the chemical elements classified in the periodic table of elements under column number 13. These elements include boron, aluminum, gallium, indium, thallium, and ununtrium.
  • trivalent dopant refers to an element or polyatomic species that substantially exists in the 3+ oxidation state when combined (e.g., doped) with a silver material. Examples of trivalent dopants include Group 13 elements, lanthanides (e.g., Yb), and polyatomic species having a +3 oxidation state.
  • the terms "divalent silver oxide” and "AgO" are used interchangeably.
  • alkaline battery refers to a primary battery or a secondary battery, wherein the primary or secondary battery comprises an alkaline electrolyte.
  • lanthanide refers to elements in a series that comprise the fourteen elements with atomic numbers 58 through 71, from cerium to lutetium.
  • AU lanthanides are f-block elements, corresponding to the filling of the 4f electron shell.
  • Lanthanum, which is a d-block element, may also be considered to be a lanthanide. All lanthanide elements form trivalent cations, Ln 3+ , whose chemistry is largely determined by the ionic radius, which decreases steadily for lanthanum to lutetium.
  • lanthanides include Lanthanum (La), Cerium (Ce), Praseodymium (Pr), Neodymium (Nd), Prom ⁇ thium (Pm), Samarium (Sm), Europium (Eu), Gadolinium (Gd), Terbium (Tb), Dysprosium (Dy). Holmium (Ho), Erbium (Er), Thulium (Tm), Ytterbium (Yb), or Lut ⁇ tium (Lu).
  • a "dopant " or “doping agent” refers io a chemical compound thai is added io a substance in low concentrations in order to alter the optical/electrical properties of the semiconductor.
  • a dopant may be added to the powder active material of a cathode to improve its electronic properties (e.g., reduce its impedance and/or resistivity or improve a cell's cycle life where the cathode, is employed in said cell).
  • doping occurs when one or more atoms of a crystal lattice of a bulk material is substituted with one or more atoms of a dopant,
  • an electrolyte refers to a substance that behaves as an electrically conductive medium.
  • the electrolyte facilitates the mobilization of electrons and cations in the cell.
  • Electrolytes include mixtures of materials such as aqueous solutions of alkaline agents. Some electrolytes also comprise additives such as buffers.
  • an electrolyte comprises a buffer comprising a borate or a phosphate.
  • Exemplary electrolytes include, without limitation, aqueous KOH, aqueous NaOH, a mixture of aqueous NaOH and KOH, or the liquid mixture of KOH, NaOH, or a combination thereof in a polymer.
  • alkaline agent refers to a base or ionic salt of an alkali metal (e.g., an aqueous hydroxide of an alkali metal). Furthermore, an alkaline agent forms hydroxide ions when dissolved in water or other polar solvents.
  • alkaline electrolytes include without limitation LiOH, NaOH, KOH, CsOH, RbOH, or combinations thereof. Electrolytes can optionally include other salts to modify the total ionic strength of the electrolyte, for example KF or Ca(OH) 2 -
  • a "cycle” or ' 'charge cycle” refers to a consecutive charge and discharge of a cell or a consecutive discharge and charge of a cell. For example, a cell undergoes one cycle when, freshly prepared, it is discharged of about 100% of its DOD and re-charged to about 100% of its SOC, In another example, a freshly prepared cell undergoes 2 cycles when the cell is:
  • Cycle 1 discharged of about 100% of its DOD and re-charged to about 100% SOC; immediately followed by
  • Cycle 2 a second discharge of about 100% of its DOD and re-charged to about 100% SOC.
  • Ah refers to Ampere (Amp) Hour and is a scientific unit denoting the capacity of a battery or electrochemical cell
  • a derivative unit, "'mAh” represents a milliamp hour and is 1/1000 of an Ah.
  • depth of discharge and “DOD” are used interchangeably to refer to the measure of how much energy has been withdrawn from a battery or cell, often expressed as a percentage of capacity, e.g., rated capacity. For example, a 100 Ah battery from which 30 Ah has been withdrawn has undergone a 30% depth of discharge (DOD).
  • state of charge' ' and “ SOC” and used interchangeably to refer to the available capacity remaining in a battery, expressed as a percentage of the cell or battery's rated capacity.
  • polyvinyliden ⁇ fluoride and its corresponding initials “PVDF” are used interchangeably as adjectives to distinguish polymers, solutions for preparing polymers, and polymer coatings, Use of these names and initials in no way implies the absence of other constituents.
  • These adjectives also encompass substituted and co- polyraerized polymers, A substituted polymer denotes one for which a substituent group, a methyl group, for example, replaces a hydrogen or fluorine on the polymer backbone.
  • polytetrafluoroethylene and its corresponding initials 'TTFE 1 ' are used interchangeably as adjectives to distinguish polymers, solutions for preparing polymers, and polymer coatings. Use of these names and initials in no way implies the absence of other constituents. These adjectives also encompass substituted and co- polynierized polymers.
  • a substituted polymer denotes one for which a substituent group, a methyl group, for example, replaces a hydrogen on the polymer backbone.
  • organic complex and “complex” refer to complexes or compounds having bonds or binding interactions (e.g., electrostatic interactions) between a metal (e.g., lead) and one or more organic ligands (e.g,, nitrate or acetate). The organic ligands often bind the metal through a heteroatom such as oxygen or nitrogen.
  • Batteries and battery electrodes are denoted with respect to the active materials in the fully-charged state.
  • a zinc-silver battery comprises an anode comprising zinc and a cathode comprising a silver powder (e.g., Ag 2 Q 3 ), Nonetheless, more than one species is present at a battery electrode under most conditions.
  • a zinc electrode generally comprises zinc metal and zinc oxide (except when fully charged), and a silver powder electrode usually comprises AgO, Ag 2 U 3 and/or Ag 2 ⁇ and silver metal (except when MIy discharged).
  • maximum voltage or “rated voltage” refers to the maximum voltage an electrochemical cell can be charged without interfering with the cell's intended utility.
  • the maximum voltage is less than about , about 2.3 V or less, or about 2.0 V).
  • the maximum voltage is less than about 15.0 V (e.g., less than about 13.0 V, or about 12.6 V or less).
  • the maximum voltage for a battery can vary depending on the number of charge cycles constituting the battery's useful life, the shelf-life of the battery, the power demands of the battery, the configuration of the electrodes in the battery, and the amount of active materials used in the battery.
  • an "anode” is an electrode through which (positive) electric current flows into a polarized electrical device.
  • the anode In a battery or galvanic cell, the anode is the negative electrode from which electrons flow during the discharging phase in the battery.
  • the anode is also the electrode that undergoes chemical oxidation during the discharging phase.
  • the anode in secondary, or rechargeable, cells, is (he electrode that undergoes chemical reduction during the cell's charging phase.
  • Anodes are formed from electrically conductive or semiconductive materials, e.g., metals, metal oxides, metal alloys, metal composites, semiconductors, or the like.
  • Anode materials include Si, Sn, Al, Ti, Mg, Fe, Bi, Zn, Sb, Ni, Pb, Li, Zr, Hg, Cd, Cu, LiC 6 , mischmetals, alloys thereof, oxides thereof, or composites thereof.
  • Anode materials such as zinc may even be sintered.
  • Anodes may have many configurations.
  • an anode may be configured from a conductive mesh or grid that is coated with one or more anode materials.
  • Li another example, an anode may be a solid sheet or bar of anode material.
  • a "cathode" is an electrode from which (positive) electric current flows out of a polarized electrical device.
  • the cathode In a battery or galvanic cell, the cathode is the positive electrode into which electrons flow during the discharging phase in the battery. The cathode is also the electrode that undergoes chemical reduction during the discharging phase. However, in secondary or rechargeable cells, the cathode is the electrode that undergoes chemical oxidation during the cell's charging phase.
  • Cathodes are formed from electrically conductive or semiconductive materials, e.g., metals, metal oxides, metal alloys, metal composites, semiconductors, or the like.
  • cathode materials include Ag, AgO, Ag 2 O 3 , Ag 2 O, HgO, Hg 2 O, CuO, CdO, NiOOH, Pb 2 O 4 , PbO 2 , IiFePO 4 , U 3 V 2 (PO 4 J 3 , V 6 O 13 , V 2 O 5 , Fe 3 O 4 , Fe 2 O 3 , MnO 2 , IiCoO 2 , LiNiO 2 , IiMn 2 O 4 , or composites thereof.
  • Cathode materials such as Ag, AgO, Ag 2 O 3 may even be sintered. Cathodes may also have many configurations.
  • a cathode may be configured from a conductive mesh that is coated with one or more cathode materials.
  • a cathode may be a solid sheet or bar of cathode material, [00049]
  • the term "electronic device” is any device that is powered by electricity.
  • electronic device can include a portable computer, a portable music player, a cellular phone, a portable video player, or any device that combines the operational features thereof.
  • cycle life is the maximum number of times a secondary battery can be cycled while retaining a capacity useful for the battery's intended use (e.g., the number of times a cell may be cycled until the cell's 100% SOC, i.e., its actual capacity, is less than 90% of its rated capacity (e.g., less than 85% of its rated capacity, about 90% of its rated capacity, or about 80% of its rated capacity), to some instances, 'cycle life' is the number of times a secondary battery or cell can be cycled until the cell's 100% SOC is at least about 60 percent of its rated capacity (e.g., at least about 70 percent of its rated capacity, at least about 80 percent of its rated capacity, at least 90 percent of its rated capacity, at least 95 percent of its rated capacity, about 90% of its rated capacity, or about 80% of its rated capacity).
  • a capacity useful for the battery's intended use e.g., the number of times a cell may be cycled until the cell's 100%
  • a zinc-silver battery comprises an anode comprising zinc and a cathode comprising a silver powder (e.g., AgO or Ag 2 O 3 ). Nonetheless, more than one species is present at a battery electrode under most conditions.
  • a zinc electrode generally comprises zinc metal and zinc oxide (except when fully charged)
  • a silver powder electrode usually comprises silver powder (e.g., AgO, Ag 2 ⁇ 3 and/or Ag 2 O and silver metal (except when fully discharged).
  • oxide applied to alkaline batteries and alkaline battery electrodes encompasses corresponding "hydroxide” species, which are typically present, at least under some conditions.
  • powder refers to a granular solid composed of a plurality of fine particles.
  • a powder's granules may flow freely when shaken or tilted, and in other instances, a powder's granules may cohere together, for example, in powders comprising a binder.
  • the term, "mean diameter” or “mean particle diameter” refers to the diameter of a sphere that has the same volume/surface area ratio as a particle of interest.
  • the terms “substantially stable” or ' 'substantiaily inert” refer to a compound or component that remains substantially chemically unchanged in the presence of an alkaline electrolyte (e.g., potassium hydroxide) and/or in the presence of an oxidizing agent (e.g., silver ions present in the cathode or dissolved in the electrolyte).
  • an alkaline electrolyte e.g., potassium hydroxide
  • an oxidizing agent e.g., silver ions present in the cathode or dissolved in the electrolyte.
  • charge profile refers to a graph of an electrochemical cell's voltage or capacity with time or cycle number.
  • resistivity refers to the internal resistance of a cathode in an electrochemical cell. This property is typically expressed in units of Ohms or micro-Ohms.
  • first and/or “second” do not refer to order or denote relative positions in space or time, but these terms are used to distinguish between two different elements or components.
  • a first separator does not necessarily proceed a second separator in time or space; however, the first separator is not the second separator and vice versa.
  • a first separator does not necessarily proceed a second separator in time or space; however, the first separator is not the second separator and vice versa.
  • a first separator does not necessarily proceed a second separator in time or space; however, the first separator is not the second separator and vice versa.
  • a second separator precedes a first separator in space or time.
  • nanometer and “nnV' are used interchangeably and refer to a unit of measure equaling IxIO "9 meters.
  • cathode active material 1' or “cathode” refer to a composition that includes silver, as described above (e.g., doped silver, coated silver, silver that is doped or coated, or any combination thereof),
  • capacity refers to the mathematical product of a cell's discharge current and the time (in hours) during which the current is discharged until the cell reaches its terminal voltage.
  • the term "actual capacity” refers to the capacity of the battery or cell when the cell has 100% SOC.
  • the capacity of a cell/battery is the amount of charge available expressed in ampere-hours (Ah)
  • An ampere is the urait of measurement used for electrical current and is defined as a coulomb of charge passing through an electrical conductor in one second.
  • the capacity of a cell or battery is related to the quantity of active materials present, the amount of electrolyte present, and the surface area of the electrodes.
  • the capacity of a battery/cell can be measured by discharging at a constant current until it reaches its terminal voltage, which depends on the cell's intended usage.
  • a cell's "rated capacity” is the capacity that a cell should theoretically discharge at 100% SOC based on the amounts of electrode materials present in the cell, the amount of electrolyte present in the cell, the surface area of the electrodes, and the cell's intended usage. For many types of cells, industry standards establish a cell's rated capacity, which is based on the cell's intended usage. [00065] II. CATHODES
  • One aspect of the present invention provides a cathode for use in an electrochemical cell comprising a silver material that is doped with a trivIER dopant to give a doped silver material, wherein the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the cathode.
  • Another aspect of the present invention provides a cathode for use in an electrochemical cell comprising a silver material that is doped with indium, aluminum, or a combination thereof, to give a doped silver material, wherein the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the cathode.
  • Another aspect of the present invention provides a cathode for use in an electrochemical eel! comprising a silver material that is doped with gallium, boron, or a combination thereof, to give a doped silver material, wherein the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the cathode.
  • the doped silver material comprises from about 0,5 wt% to about 5 wt% of trivIER dopant. In other embodiments above, the doped silver material comprises from about 1 wt% to about 8 wt% of trivending dopant.
  • the silver material of the cathode comprises a powder.
  • the powder has a mean particle diameter of about 20 ⁇ m or less (e.g., 15 ⁇ m or less, or 10 ⁇ m or less). In other instances, the powder has a mean particle diameter of about 15 ⁇ m or less (e.g., 10 ⁇ m or less). In other instances, the powder has a mean particle diameter of about 5 ⁇ m or less.
  • the doped silver material comprises Ag, AgO, AgO, Ag 2 O 3 , AgOH, AgOOH, AgONa, AgCuO 2 , AgFeO 2 , AgMnO 2 , Ag(OH) 2 , or any combination thereof.
  • die cathode further comprises a binder.
  • the cathode comprises a binder and the binder comprises PTFE or PVDF.
  • One aspect of the present invention provides a cathode for use in an electrochemical cell comprising a silver material comprising a dopant, wherein the dopant comprises indium, aluminum, or a combination thereof, and the dopant is present in a sufficient concentration such that cathode has a resistivity of about 500hm*cm or less.
  • the dopant is present in a sufficient concentration such that cathode has a resistivity of about 40 Ohm'cm or less.
  • the dopant is present in a sufficient concentration such that cathode has a resistivity of about 35 0hm*cm or less.
  • the dopant is present in a sufficient concentration such that cathode has a resistivity of about 30 Ohm*cm or less.
  • the cathode comprises from about 0.25 wt% to about 10 wt% of dopant.
  • the cathode comprises from about 0.75 wt% to about 9 wt% of dopant.
  • the cathode comprises from about 1 wt% to about 8 wt% of dopant
  • the cathode comprises from about 0.5 wt% to about 5 wt% of dopant.
  • cathodes of the present invention comprise a silver material.
  • the silver material includes bulk material that may be doped with a dopant, as provided herein, or the silver material may comprise a powder.
  • the powder may be doped or coated (e.g., a plurality of the granuals of silver material comprising the powder are doped with a dopant). Furthermore, the powder may undergo further processing (e.g., hot pressing, or the like) to generate a silver bulk material that is useful in cathodes of the present invention.
  • the cathode comprises a silver powder that is doped with a dopant, wherein the doped silver powder has a mean particle diameter of about 15 ⁇ m or less.
  • the doped silver powder has a mean particle diameter of about 10 ⁇ m or less.
  • the doped silver powder has a mean particle diameter of about 7 ⁇ m or less.
  • the doped silver powder has a mean particle diameter of about 5 ⁇ m or less.
  • the cathodes comprise silver material (e.g., silver powder) and the silver material comprises Ag, AgO, Ag 2 O, Ag 2 Oa, AgOH, AgOOH, AgONa, AgCuO 2 , AgFeO 2 , AgMnO 2 , Ag(OH) 2 , hydrates thereof, or any combination thereof.
  • the cathode comprises silver material (e.g., silver powder), which comprises AgO.
  • the silver powder comprises Ag 2 Oa.
  • Cathodes of the present invention can optionally comprise additives such as binders, or other additives to improve one or more features of the cathode.
  • the cathode comprises a binder.
  • Suitable binders include any binder that is substantially inert to the silver oxide powder or doped silver oxide powder.
  • the binder comprises
  • a cathode for use in an electrochemical cell comprising a silver powder doped with a sufficient concentration of indium such that cathode has a resistivity of about 30 Ohm»cm or less; and the doped silver powder has a mean particle diameter of about 7 ⁇ m or less.
  • a cathode for use in an electrochemical cell comprising a silver powder doped with a sufficient concentration of aluminum such that cathode has a resistivity of about 30 Ohm » cm or less; and the doped silver powder has a mean particle diameter of about 7 ⁇ m or less.
  • a cathode comprises a silver powder that is doped with a sufficient amount of aluminum, indium, or a combination thereof to provide a resistivity of about 30 Ohm'cm or less and has a mean particle diameter of about 7 ⁇ m or less, wherein the silver powder comprises Ag, AgO, Ag 2 O, Ag 2 Qs, AgOH, AgOOH, AgONa, AgCuO 2 ,
  • cathodes of the present invention can optionally comprise additives such as binders, current collectors, or the like.
  • the cathode of the present invention comprises a binder.
  • the cathode comprises a binder, and the binder comprises PTFE, PVDF (e.g. f PVDF-co-HFP), CMC, PVP, PAA, or a copolymer thereof.
  • cathodes of the present invention comprise silver powder.
  • Silver powder includes Ag, AgO, Ag 2 O, Ag 2 Oj, AgOH, AgOOH, AgONa, AgCuO 2 , AgFeO 2 ,
  • Another aspect of the present invention provides a cathode for use in an electrochemical cell comprising a silver powder comprising a dopant, wherein the dopant comprises aluminum, and the dopant is present in a sufficient concentration such that cathode has a resistivity of about 40 Ohnrem or less.
  • the cathode comprises from about 0.2S wt% to about 10 wt% of dopant, i.e., aluminum.
  • the cathode comprises from about O.S wt% to about S wt% of dopant, i.e., aluminum.
  • the cathode comprises from about 1 wt% to about 8 wt% of dopant, i.e., aluminum.
  • the cathode comprises a doped silver powder that has a mean particle diameter of about 20 ⁇ m or less. In some embodiments, the cathode comprises a doped silver powder that has a mean particle diameter of about 15 ⁇ m or less. For example, the doped silver powder has a mean particle diameter of about 5 ⁇ m or less. [00086] In another embodiment, the dopant is present in a sufficient concentration such that cathode has a resistivity of about 30 Ohnvcm or less.
  • Cathodes of the present invention comprise silver oxide.
  • the cathode comprises silver powder comprising Ag, AgO, Ag 2 ⁇ , Ag 2 Os, AgOH, AgOOH, AgONa, AgCu ⁇ 2 , AgFeO 2 , AgMnO 2 , Ag(OH) 2 , hydrates thereof, or any combination thereof.
  • the silver powder comprises Ag 2 Oa.
  • the silver powder comprises AgO.
  • Cathodes of the present invention can optionally comprise additives such as binders, or other additives to improve one or more features of the cathode.
  • the cathode comprises a binder.
  • Suitable binders include any binder that is substantially inert to the silver oxide powder or doped silver oxide powder.
  • the binder comprises PTFE or PVDF.
  • a cathode for use in an electrochemical cell comprising a doped silver powder comprising a dopant, wherein the dopant comprises aluminum, and the dopant is present in a sufficient concentration such that cathode has a resistivity of about 30 Ohm*cm or less; and the doped silver oxide powder has a mean particle diameter of about S ⁇ m or less.
  • a cathode comprises a silver powder that is doped with a sufficient amount of aluminum to provide a resistivity of about 30 Ohnvcm or less and has a mean particle diameter of about 5 ⁇ m or less, wherein the silver powder comprises AgO, Ag 2 ⁇ 3 , or any combination thereof.
  • cathodes of the present invention can optionally comprise additives such as binders, current collectors, or the like.
  • the cathode of the present invention comprises a binder.
  • the cathode comprises a binder, and the binder comprises PTFE, PVDF (e.g., PVDF-co-HFP), CMC, PVP, PAA, or a copolymer thereof.
  • cathodes of the present invention comprise silver oxide powder.
  • Silver powder includes Ag, AgO, Ag 2 O, Ag 2 Os, AgOH, AgOOH, AgONa, AgCuO 2 , AgFeO 2 , AgMnO 2 , Ag(OH) 2 , hydrates thereof, or any combination thereof.
  • Another aspect of the present invention provides a method of producing a cathode for use in an electrochemical cell comprising providing a silver powder that is doped with from about 0.25 wt% to about 10 wt% of a trivalent dopant by weight of the cathode to give a doped silver powder; and forming the doped silver powder into a cathode.
  • Another aspect of the present invention provides a method of producing a cathode for use in an electrochemical cell comprising providing a silver powder that is doped with from about 0.25 wi% to about 10 wt% of a dopant comprising at least one Group 13 element by weight of the cathode to give a doped silver powder; and forming the doped silver powder into a cathode,
  • Another aspect of the present invention provides a method of producing a cathode for use in an electrochemical cell comprising providing a silver powder that is doped with from about 0.25 wt% to about 10 wt% of a dopant comprising gallium, boron, indium, aluminum, or any combination thereof by weight of the cathode to give a doped silver powder; and forming the doped silver powder into a cathode.
  • Another aspect of the present invention provides a method of producing a cathode for use in an electrochemical DC! comprising providing a silver powder that is doped with from about 0.25 wt% to about 10 wt% of a dopant comprising gallium, boron, or a combination thereof to give a doped silver powder; and forming the doped silver powder into
  • Another aspect of the present invention provides a method of producing a cathode for use in an electrochemical cell comprising providing a silver powder that is doped with from about 0.25 wt% to about 10 wt% of a dopant comprising indium, aluminum, or a combination thereof to give a doped silver powder; and forming the doped silver powder into a cathode.
  • the doped silver powder comprises from about 0.5 wt% to about 5 wt% of dopant. In several embodiments of the methods above, the doped silver powder comprises from about 1 wt% to about 8 wt% of dopant. In others, the doped silver powder has a mean particle diameter of about 20 ⁇ m or less. And, in some embodiments, the doped silver powder has a mean particle diameter of about 15 ⁇ rn or less. For instance, the doped silver powder has a mean particle diameter of about 5 ⁇ m or less.
  • the silver powder comprises Ag, AgO, Ag 2 O, Ag 2 O 3 , AgOH, AgOOH, AgONa, AgCuO 2 , AgFeO 2 , AgMnO 2 , Ag(OH) 2 , or any combination thereof.
  • the silver powder comprises AgO, Ag 2 O, Agj €> 3 , or any combination thereof.
  • the dopant comprises gallium, boron, indium, aluminum, thallium, or any combination thereof.
  • the dopant comprises gallium, boron, or a combination thereof.
  • the dopant comprises indium, aluminum, or a combination thereof.
  • Some embodiments of the methods above further comprise the step of providing a binder.
  • the method further includes providing a binder and the binder comprises PTFE or PVDF.
  • Another aspect of the present invention provides methods of manufacturing a cathode comprising providing a silver powder; and doping the silver powder (e.g., Ag, AgO,
  • the silver powder is doped with a sufficient amount of dopant such that the cathode has a resisitivity of about 40 Ohm*cm or less.
  • the silver powder is doped with a sufficient amount of dopant such that the cathode has a resisitivity of about 35 Ohm «cm or less.
  • the silver powder is doped with a sufficient amount of dopant such that the cathode has a resisitivity of about 30 Ohm»cm or less.
  • the silver powder is doped with from about 0.25 wt% to about
  • the silver powder is doped with from about 1 wt% to about
  • the doped silver powder has a mean particle diameter of about
  • the doped silver powder has a mean particle diameter of about 5 ⁇ m or less.
  • the silver powder comprises AgO.
  • the silver oxide powder comprises Ag 2 Os.
  • Methods of the present invention can optionally include providing cathode additives.
  • One exemplary method includes further comprising providing a binder.
  • Suitable binders include any of those mentioned herein.
  • the binder comprises PTFE or
  • Another aspect of the present invention provides methods of manufacturing a cathode comprising providing a silver powder; and doping the silver powder with a sufficient amount of dopant such that cathode has a resistivity of about 30 Ohm*cm or less, wherein the dopant comprises aluminum.
  • the silver powder is doped with from about 0.25 wt% to about 10 wt% of dopant.
  • the silver powder is doped with from about 1 wt% to about 8 wt% of dopant,
  • the doped silver powder has a mean particle diameter of about 15 ⁇ m or less.
  • the doped silver powder has a mean particle diameter of about 5 ⁇ m or less.
  • the silver powder comprises AgO.
  • the silver oxide powder comprises Ag 2 ⁇ 3 .
  • Methods of the present invention can optionally include providing cathode additives, One exemplary method includes further comprising providing a binder.
  • Suitable binders include any of those mentioned herein.
  • the binder comprises PTFE or
  • One aspect of the present invention provides an electrochemical cell comprising a cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein, the dopant comprises a trivalent dopant, and the dopant is present in a sufficient concentration to impart the cell with an actual capacity of at least about 80% (e.g., at least about 85%, or at least about 90%) of the cell's rated capacity over at least 100 cycles (e.g., at least 200 cycles, at least 250 cycles, at least 300 cycles, or at least 400 cycles).
  • the dopant comprises a trivalent dopant
  • the dopant is present in a sufficient concentration to impart the cell with an actual capacity of at least about 80% (e.g., at least about 85%, or at least about 90%) of the cell's rated capacity over at least 100 cycles (e.g., at least 200 cycles, at least 250 cycles, at least 300 cycles, or at least 400 cycles).
  • Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein the dopant comprises a trivalent dopant, and the dopant is present in a sufficient concentration to impart the cell with an actual capacity of at least about 60% of the cell's rated capacity over at least about 80 cycles.
  • Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein the dopant comprises at least one Group 13 element, and the dopant is present in a sufficient concentration to impart the cell with an actual capacity of at least about 80% (e.g., at least about 85%, or at least about 90%) of the cell's rated capacity over at least 100 cycles (e.g., at least 200 cycles, at least 250 cycles, at least 300 cycles, at least 350 cycles, or at least 400 cycles).
  • the dopant comprises at least one Group 13 element
  • the dopant is present in a sufficient concentration to impart the cell with an actual capacity of at least about 80% (e.g., at least about 85%, or at least about 90%) of the cell's rated capacity over at least 100 cycles (e.g., at least 200 cycles, at least 250 cycles, at least 300 cycles, at least 350 cycles, or at least 400 cycles).
  • Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein the dopant comprises gallium, boron, indium, aluminum, thallium, or any combination thereof, and the dopant is present in a sufficient concentration to impart the cell with an actual capacity of at least about 80% (e.g., at least about 85%, or at least about 90%) of the cell's rated capacity over at least 100 cycles (e.g., at least 200 cycles, at least 250 cycles, at least 300 cycles, at least 350 cycles, or at least 400 cycles).
  • the dopant comprises gallium, boron, indium, aluminum, thallium, or any combination thereof, and the dopant is present in a sufficient concentration to impart the cell with an actual capacity of at least about 80% (e.g., at least about 85%, or at least about 90%) of the cell's rated capacity over at least 100 cycles (e.g., at least
  • Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising a silver materia! comprising a dopant; and an anode comprising zinc, wherein the dopant comprises gallium, boron, or a combination thereof, and the dopant is present in a sufficient concentration to impart the cell with an actual capacity of at least about 80% (e.g., at least about 85%, or at least about 90%) of the cell's rated capacity over at least 100 cycles (e.g., at least 200 cycles, at least 250 cycles, at least 300 cycles, at least 350 cycles, or at least 400 cycles),
  • Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein the dopant comprises aluminum, indium, or a combination thereof, and the dopant is present in a sufficient concentration to impart the cell with an actual capacity of at least about 80% (e.g., at least about 85%, or at least about 90%) of the cell's rated capacity over at least 100 cycles (e.g., at least, 200 cycles, at least 250 cycles, at least 300 cycles, at least 350 cycles, or at, least 400 cycles).
  • the dopant comprises aluminum, indium, or a combination thereof
  • the dopant is present in a sufficient concentration to impart the cell with an actual capacity of at least about 80% (e.g., at least about 85%, or at least about 90%) of the cell's rated capacity over at least 100 cycles (e.g., at least, 200 cycles, at least 250 cycles, at least 300 cycles, at least 350 cycles, or
  • the silver material comprises from about 0.25 wl% to about 10 wt % of trivalent dopant (e.g., at least one Group 13 element (e.g., thallium, boron, gallium, indium, aluminum, or any combination thereof)). In some embodiments, the silver material comprises from about 0.5 wt% to about 5 wt % of trivalent dopant (e.g., at least one Group 13 element (e.g., thallium, boron, gallium, indium, aluminum, or any combination thereof)).
  • trivalent dopant e.g., at least one Group 13 element (e.g., thallium, boron, gallium, indium, aluminum, or any combination thereof)).
  • the silver material comprises a powder
  • the silver material comprises a powder and the powder has a mean particle diameter of about 20 ⁇ m or less (e.g., 15 ⁇ m or less, 10 ⁇ m or less). In other instances, the powder has a mean particle diameter of about 5 ⁇ m or less.
  • the silver powder comprises Ag, AgO, AgyQ, Ag 2 O 3 , AgOH, AgOOH, AgONa, AgCuO 2 , AgFeO 2 , AgMnO 2 , Ag(OH) 2 , or any combination thereof.
  • the silver powder comprises AgO, Ag 2 O, Ag 2 O 3 , or any combination thereof.
  • the silver material comprises AgO.
  • the silver material comprises Ag 2 ⁇ .
  • the silver material comprises a dopant wherein the dopant comprises gallium, boron, indium, aluminum, or any combination thereof.
  • the silver material comprises a dopant wherein the dopant comprises gallium, boron, or a combination thereof.
  • the silver material comprises a dopant wherein the dopant comprises indium, aluminum, or a combination thereof.
  • the cathode, the anode, or both comprise a binder.
  • the cathode comprises a binder.
  • the cathode comprises a binder and the binder comprises PTFE or PVDF.
  • the anode comprises a binder.
  • the anode comprises a binder, and the binder comprises PTFE or PVDF.
  • Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising silver powder comprising from about 0.2S wt% to about 10 wt% of a trivalent dopant; an anode comprising zinc; and an electrolyte comprising KOH.
  • Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising silver powder comprising from about 0.2S wt% to about 10 wt% of at least one Group 13 element by weight of the cathode; an anode comprising zinc; and an electrolyte comprising KOH.
  • Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising silver powder comprising from about 0.25 wt% to about 10 wt% of a dopant; an anode comprising zinc; and an electrolyte comprising KOH, wherein the dopant comprises gallium, boron, indium, aluminum, thallium, or any combination thereof.
  • Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising silver powder comprising from about 0.2S wt% to about 10 wt% of a dopant; an anode comprising zinc; and an electrolyte comprising KOH, wherein the dopant comprises gallium, boron, or a combination thereof.
  • an electrochemical cell comprising a cathode comprising silver powder comprising from about 0.25 wt% to about 10 wt% of a dopant; an anode comprising zinc; and an electrolyte comprising KOH 1 wherein the dopant comprises indium, aluminum, or a combination thereof.
  • the silver material comprises a powder.
  • silver material comprises a powder, and the powder has a mean particle diameter of about 15 ⁇ m or less. In other instances, the powder has a mean particle diameter of about 5 ⁇ m or less.
  • the silver powder comprises Ag, AgO, Ag 2 O, Ag 2 O 3 , AgOH, AgOOH, AgONa, AgCuO 2 , AgFeO 2 , AgMnO 2 , Ag(OH) 2 , or any combination thereof.
  • the silver powder comprises AgO, Ag 2 O, Ag 2 Os, or any combination thereof .
  • the silver material comprises AgO.
  • the silver material comprises Ag 2 O.
  • the cathode, the anode, or both comprise a binder.
  • the cathode comprises a binder.
  • cathode comprises a binder, and the binder comprises PTFE or PVDF.
  • the anode comprises a binder.
  • the anode comprises a binder, and the binder comprises PTFE or
  • the cell further comprises an electrolyte comprising NaOH, KOH, or a combination thereof.
  • One aspect of the present invention provides an electrochemical cell comprising a cathode comprising silver powder and a first binder; and an anode comprising zinc and a second binder, wherein the doped silver powder comprises a sufficient amount of indium, aluminum, or a combination thereof to impart the cathode with a resistivity of about SO
  • One aspect of the present invention provides an electrochemical cell comprising a cathode comprising doped silver powder and a first binder; and an anode comprising zinc and a second binder, wherein the doped silver powder comprises a sufficient amount of indium to impart die cathode with a resistivity of about 30 Ohm «cm or less.
  • any of the cathodes described herein are suitable for use in electrochemical cells of the present invention.
  • the electrochemical comprises an electrolyte comprising
  • the electrochemical cell comprises a cathode comprising doped silver oxide powder comprising from about 0.25 wt% to about 10 wt% of a dopant comprising aluminum and a first binder; an anode comprising zinc and a second binder, and an electrolyte comprising KOH, wherein the cathode has a resistivity of about 30 Ohm • cm or less.
  • One aspect of the present invention provides an electrochemical cell comprising a cathode comprising doped silver powder and a first binder; and an anode comprising zinc and a second binder, wherein the doped silver powder comprises a sufficient amount of aluminum to impart the cathode with a resistivity of about 30 Ohm»cm or less.
  • any of the cathodes described herein are suitable for use in electrochemical cells of the present invention.
  • the electrochemical comprises an electrolyte comprising
  • the electrochemical cell comprises a cathode comprising doped silver powder comprising from about 0.25 wt% to about 10 wt% of a dopant comprising aluminum and a first binder; an anode comprising zinc and a second binder; and an electrolyte comprising KOH, wherein the cathode has a resistivity of about 30 ⁇ hm* ⁇ n or less.
  • Cathodes and anodes of electrochemical ceils of the present invention can optionally include additives such as a binder, a current collector, or the like.
  • the binder of the cathode and the binder of the anode can include the same material or different materials,
  • the binder of the anode or the cathode comprises PTFE, PVDF, or any copolymer thereof.
  • I ⁇ cathodes comprising a binder
  • the binder is admixed with die doped silver powder in a suitable concentration (e.g., less than 10 wt% of binder by weight of the cathode, (e.g., 5 wt% or less of binder by weight of the cathode)) and formed into dough-like material that is shaped to provide the cathode with a suitable size and geometry.
  • a suitable concentration e.g., less than 10 wt% of binder by weight of the cathode, (e.g., 5 wt% or less of binder by weight of the cathode)
  • anodes may likewise be produced using a binder.
  • Electrochemical cells of the present invention additionally comprise a separator that is separates the anode from the cathode.
  • Separators of the present invention can comprise a film having a single layer or a plurality of layers, wherein the plurality of layers may comprise a single polymer (or copolymer) or more than one polymer (or copolymer).
  • the separators comprise a unitary structure fomi ⁇ d from at least two strata.
  • the separator can include strata wherein each layer comprises the same material, or each layer comprises a different layer, or the strata are layered to provide layers of the same material and at least on layer of another material.
  • one stratum comprises an oxidation resistant material, and the remaining stratum comprises a dendrite resistant material.
  • at least one stratum comprises an oxidation-resistant material, or at least one stratum comprises a dendrite-resi&tant material.
  • the unitary structure is fo ⁇ ned when the material comprising one stratum (e.g., an oxidation- resistant material) is coextruded with the material comprising another stratum (e.g., a dendrite resistant material or oxidation-resistant material).
  • the unitary separator is formed from the coextrasion of oxidation-resistant material with dendrit ⁇ - resistant material. [000145] In several embodiments, the oxidation-resistant materia!
  • separators useful in electrochemical cells can be configured in any suitable way such thai the separator is substantially inert in the presence of the anode, cathode and electrolyte of the electrochemical cell,
  • a separator for a rectangular battery electrode may be in the form of a sheet or film comparable in size or slightly larger than the electrode, and may simply be placed on the electrode or may be sealed around the edges.
  • the edges of the separator may be sealed to the electrode, an electrode current collector, a battery case, or another separator sheet or film on the backside of the electrode via an adhesive sealant, a gasket, or fusion (heat sealing) of the. separator or another material.
  • the separator may also be in the form of a sheet or film wrapped and folded around the electrode to form a single layer (front and back), an overlapping layer, or multiple layers.
  • the separator may be spirally wound with the electrodes in a jelly-roll configuration.
  • the separator is included in an electrode stack comprising a plurality of separators.
  • the oxidation-resistant separator of the invention may be incorporated in a battery in any suitable configuration.
  • the oxidation-resistant stratum of the separator comprises a polyether polymer material that is coextruded with a dendrite- resistant material.
  • the polyether material can comprise polyethylene oxide (PEO) or polypropylene oxide (PPO), or a copolymer or a mixture thereof.
  • the polyether material may also be copolymerized or mixed with one or more other polymer materials, polyethylene, polypropylene and/or polytetrafluoroethylene (PTFE), for example.
  • the PE material is capable of forming a free-standing polyether film when extruded alone, or can form a free standing film when coextruded with a dendrite-resistani material.
  • the polyether material is substantially inert in the alkaline battery electrolyte and in the presence of silver ions.
  • the oxidation resistant material comprises a PE mixture that optionally includes zirconium oxide powder.
  • zirconium oxide powder inhibits silver ion transport by forming a surface complex with silver ions.
  • zirconium oxide encompasses any oxide of zirconium, including zirconium dioxide and yttria-stabilized zirconium oxide.
  • the zirconium oxide powder is dispersed throughout the PE material so as to provide a substantially uniform silver complexation and a uniform barrier to transport of silver ions.
  • the average particle size of the zirconium oxide powder is in the range from about J nm to about 5000 nm, e.g., from about 5 nm to about 100 nm.
  • the oxidation-resistant materia! further comprises an optional conductivity enhancer.
  • the conductivity enhancer can comprise an inorganic compound, potassium titanate, for example, or an organic material. Titanates of other alkali metals than potassium may be used. Suitable organic conductivity enhancing materials include organic sulfonates and carboxylates. Such organic compounds of sulfonic and carboxylic acids, which may be used singly or in combination, comprise a wide range of polymer materials that may include salts formed wiih a wide variety of electropositive cations, K + , Na + , Li + , Pb +?
  • the conductivity enhancer may include a sulfonate or carboxylate copolymer, with polyvinyl alcohol, for example, or a polymer having a 2-acrylamido-2-methyl propanyl as a functional group. A combination of one or more conductivity enhancing materials can be used.
  • Oxidation-resistant material that is coextruded to form a separator of the present invention can comprise from about 5 wt % to about 95 wt % (e.g., from about 20 wt % to about 60 wt %, or from about 30 wt % to about 50 wt %) of zirconium oxide and/or conductivity enhancer.
  • Oxidation-resistant materials can also comprise additives such as surfactants that improve dispersion of the zirconium oxide powder by preventing agglomeration of small particles.
  • Any suitable surfactant may be used, including one or more anionic, cationic, non- ionic, ampholytic, amphoteric and zwitterionic surfactants, and mixtures thereof.
  • the separator comprises an anionic surfactant.
  • the separator comprises an anionic surfactant, and the anionic surfactant comprises a salt of sulfate, a salt of sulfonate, a salt of carboxylate, or a salt of sareosinate.
  • One useful surfactant comprises p- (l,l,3,3-tetramethylbutyl)-phenyl ether, which is commercially available under the trade name Triton X- 100 from Rohm and Haas.
  • the oxidation-resistant material comprises from about 0.01 wt % to about 1 wt % of surfactant. [000154] 2. Polyvinyl Polymer Material
  • the dendrite-resistant stratum of the separator comprises a polyvinyl polymer material that is coextruded with the oxidation- resistant material.
  • the PVA material comprises a cross-linked polyvinyl alcohol polymer and a cross-linking agent.
  • the cross-linked polyvinyl alcohol polymer is a copolymer
  • the cross-linked PVA polymer is a copolymer comprising a first monomer, PVA, and a second monomer.
  • the PVA polymer is a copolymer comprising at least 60 mole percent of PVA and a second monomer.
  • the second monomer comprises vinyl acetate, ethylene, vinyl butyral, or any combination thereof.
  • PVA material useful in separators of the present invention also comprise a cross- linking agent in a sufficient quantity as to render the separator substantially insoluble in water.
  • the cross-Sinking agent used in the separators of the present invention comprises a monoaldehyde (e.g., formaldehyde or glyoxilic acid); aliphatic, furyl or aryl dialdehydes (e.g., glutaraidchyde, 2,6 furyldialdehyde or terephthaldehyde); dicarboxylic acids (e.g., oxalic acid or succinic acid); polyisocyanates; methylolmelamine; copolymers of styrene and maleic anhydride; germaic acid and its salts; boron compounds (e.g., boron oxide, boric acid or its salts; or metaboric acid or its salts); or salts of copper, zinc, aluminum or titanium.
  • a monoaldehyde e.g
  • the cross-linking agent comprises boric acid.
  • the PVA material optionally comprises zirconium oxide powder.
  • the PVA material comprises from about 1 wt % to about 99 wt % (e.g., from about 2 wt % to about 98 wt %, from about 20 wt % to about 60 wt %, or from about 30 wt % to about 50 wt %).
  • the dendrite-resistant strata of the separator of the present invention comprises a reduced ionic conductivity.
  • the separator comprises an ionic resistance of less than about 20 rn ⁇ /cm ⁇ , (e.g., less than about 10 m ⁇ /cm 2 , less than about 5 m ⁇ /cra 2 , or less than about 4m ⁇ /cm 2 ).
  • the PVA material that forms the dendrite-resistant stratum of the separator of the present invention can optionally comprise any suitable additives such as a conductivity enhancer, a surfactant, a plasticizer, or the like.
  • the PVA material further comprises a conductivity enhancer.
  • the PVA material comprises a cross-linked polyvinyl alcohol polymer, a zirconium oxide powder, and a conductivity enhancer.
  • the conductivity enhancer comprises a copolymer of polyvinyl alcohol and a hydroxyl-conducting polymer. Suitable hydroxyl-conducting polymers have functional groups that facilitate migration of hydroxyl ions.
  • the hydroxyl- conducting polymer comprises polyacrylate, polylactone, polysulfonate, polycarboxylate, polysulfate, polysarconate, polyaraide. polyamidosulfonate, or any combination thereof.
  • a solution containing a copolymer of a polyvinyl alcohol and a poiylactone is sold commercially under the trade name Vytek polymer by Celanese, Inc.
  • the separator comprises from about 1 wt % to about 10 wi % of conductivity enhancer,
  • the PVA material further comprises a surfactant.
  • the separator comprises a cross-linked polyvinyl alcohol polymer, a zirconium oxide powder, and a surfactant.
  • the surfactant comprises one or more surfactants selected from an anionic surfactant, a catioiiic surfactant, a nonionic surfactant, an ampholytic surfactant, an amphoteric surfactant, and a zwitterionic surfactant.
  • surfactants are commercially available, ⁇ n several examples, the PVA material comprises from about 0.01 wt % to about 1 wt % of surfactant.
  • the dendrite-resistant stratum further comprises a plasticizer.
  • the dendrite-resistant stratum comprises a cross-linked polyvinyl alcohol polymer, a zirconium oxide powder, and a plasticizer.
  • the plasticizer comprises one or more plasticizers selected from glycerin, low-molecular-weight polyethylene glycols, aminoalcohols, polypropylene glycols, 1,3 pentanediol branched analogs, 1,3 pentanediol, and/or water.
  • the plasticizer comprises greater than about 1 wt % of glycerin, low- molecular- weight polyethylene glycols, aminoalcohols, polypropylene glycols, 1,3 pentanediol branched analogs, 1,3 pentanediol. or any combination thereof, and less than 99 wt % of water.
  • the plasticizer comprises from about 1 wt % to about 10 wt % of glycerin, low-molecular-weight polyethylene glycols, aminoalcohols, polypropylene glycols, 1,3 pentanediol branched analogs, 1,3 pentanediol, or any combination thereof, and from about 99 wt % to about 90 wt % of water.
  • the separator of the present invention further comprises a plasticizer.
  • the plasiicizer comprises glycerin, a low-molecular-weight polyethylene glycol, an aminoalcohol, a polypropylene glycols, a 1.3 pentanediol branched analog, 1.3 pentanediol, or combinations thereof, and/or water. [0 ⁇ 0165] C. Ejectrolylgs
  • Electrochemical cells of the present invention can comprise any suitable electrolyte.
  • the electrochemical cell comprises an electrolyte that includes aqueous NaOH or KOH.
  • the electrolyte comprises a mixture of NaOH or KOH and a liquid PEO polymer.
  • Electrolytes that are suited to electrochemical cells of the present invention include an alkaline agent.
  • Exemplary electrolytes include aqueous metal-hydroxides such as NaOH and/or KOH.
  • Other exemplary electrolytes include mixtures of a metal hydroxide and a polymer that has a glass transition temperature below the range of operating and/or storage temperatures for the electrochemical cell into which it employed (e.g. at least -20 0 C).
  • Polymers useful far formulating an electrolyte of the present invention are also at least substantially miscible with an alkaline agent.
  • the polymer is at least substantially miscible with the alkaline agent over a range of temperatures that at least includes the operating and storage temperatures of the electrochemical device in which the mixture is used.
  • the polymer is at least substantially miscible, e.g., substantially miscible with the alkaline agent at a temperature of at least -20 0 C.
  • the electrolyte has a glass transition temperature of at least -IS 0 C (e.g., at least -12 0 C, at least - 10 0 C, or from about -20 0 C to about 70 0 C).
  • the polymer is at least substantially miscible with the alkaline agent at a temperature from about -20 0 C to about 60 0 C.
  • the polymer is at least substantially miscible with the alkaline agent at a temperature of from about -10 0 C to about 6O 0 C.
  • the polymer can combine with the alkaline agent at a temperature in the range of temperatures of the operation of the electrochemical device in which is it stored to form a solution.
  • the electrolyte comprises a polymer of formula (I):
  • each of Ri, R 2 , R 3 , and R 4 is independently (Vi-Qi-V 2 -Q 2 -V 3 -Q 3 ) B1 each of Vi, V 2 , and V 3 , is independently a bond or -O-, each of Qi, Q 2 , and Qj, is independently a bond, hydrogen, or a CMJ linear or branched unsubstituted alkyl, n is 1-5, and p is a positive integer of sufficient value such that the polymer of formula (I) has a total molecular weight of less than 10,000 amu (e.g., less than about SOOO amu, less than about 3000 amu, from about SO amu to about 2000 amu, or from about 100 amu to about 1000 amu) and an alkaline agent.
  • 10,000 amu e.g., less than about SOOO amu, less than about 3000 amu, from about SO amu to about 2000 amu, or from about 100 amu to about 1000 amu
  • the polymer is straight or branched.
  • Ri is independently (Vi-Qi-V 2 -Qz-Vs-Qj) n , wherein n is 1, each of Vi, Qi, V 2 , Q 2 , and V 3 is a bond, and Qj is hydrogen.
  • R4 is independently (Vi-Qi-Va-Qj-V 3 -Qj) n , wherein n is 1, each of V], Qi, V 2 , Q 2 , and V 3 , is a bond, and Q 3 is hydrogen.
  • both of Ri and R4 are (Vi- Qi-V 2 -Q2-V 3 -Qj)n, each n is 1, each of Vj, Qi, V 2 , Q 2 , and V 3 is a bond, and each Q 3 is hydrogen.
  • Rt is independently (Vi-Qi-V 2 -Q 2 -V 3 -Qs) n , wherein n is 1, each of Vi, Qi, V 2 , Q 2 , and V 3 is abond, and Q 3 is -CH 3 , -CH 2 CH 3 , -
  • Ri is independently (Vi-Q 1 -V 2 -Ch-V 3 -Qs)Ii, wherein n is I 1 each of Vi, Qi, V 2 , Q 2 , and V 3 is a bond, and Q 3 is -CH 3 or H.
  • Ri is independently (VrQi-V 2 -Q 2 -VB-Qs) n .
  • n is 1, one of Qi or Q 2 is -CH 2 -, -CH 2 CH 2 -, or -CH 2 CH 2 CH 2 -; Vi and V 2 are each a bond; V 3 is -O-, and
  • R4 is independently (Vi-Qi-V 2 -Ch-Vs-Qs) n , wherein n is
  • each of Vi, Qi, V 2 , Q 2 is a bond, and V 3 is -O- or a bond, and Q 3 is hydrogen, -CH 3 , -
  • R 4 is independently (Vi-Qi-V 2 -Q 2 -V 3 -Q 3 ) B , wherein n is I 1 each of Vi, Qi, V 2 , Q 2 , and V 3 is a bond, and Q 3 is -H, -CH 3 , -CH 2 CH 3 , or -
  • Ri is (Vi-QrV 2 -Q 2 -V 3 -Qs) n , wherein n is 1, each of Vi,
  • Qi, V 2 , Q 2 , and V 3 is a bond, and Q 3 is -CH 3 , and R 4 is (VrQi-V 2 -Q 2 -V 3 -Q 3 ),,, wherein n is 1, each of Vi, Qi, V 2 , Q 2 , is a bond, and V 3 is -O-, and Q 3 is -H.
  • R 2 is independently (VrQi-V 2 -Q 2 -V 3 -Q 3 )Q, wherein n is 1, each of Vi, Qi, V 2 , Q 2 , and V 3 is a bond, and Q 3 is -CH 3 , -CH 2 CH 3 , -CH 2 CH 2 CH 3 , or H.
  • R 2 is independently (V]-QrV 2 -Ch-V 3 -Q 3 ),, wherein n is 1, one of Vi, Qi,
  • V 2 , Q 2 , and V 3 is -O-, and Q 3 is -H.
  • R 3 is independently (VrQi-V 2 -Q 2 -V 3 -Q 3 ),, wherein n is I 1 each of Vi, Qi, V 2 , Q 2 , and V 3 is a bond, and Q 3 is -CH 3 , -CH 2 CH 3 , -CH 2 CH 2 CH 3 , or H.
  • R 3 is independently (VrQi-Va-Ch-V 3 -Qj) n , wherein n is 1, one of Vi, Q],
  • V 2 , Q 2 , and V 3 is -O-, and Q 3 is -H.
  • the polymer comprises a polyethylene oxide.
  • the polymer comprises a polyethylene oxide selected from polyethylene glycol, polypropylene glycol, polybutylene glycol, alkyl-polyethylene glycol, alkyl-polypropylene glycol, alkyl-polybutylene glycol, and any combination thereof.
  • the polymer is a polyethylene oxide having a molecular weight or mean molecular weight of less than about 10,000 amu (e.g., less than about 5000 amu, or from about 100 amu to about 1000 amu). In other embodiments, the polymer comprises polyethylene glycol.
  • Alkaline agents useful in the electrolyte of the present invention are capable of producing hydroxyl ions when mixed with an aqueous or polar solvent such as water and/or a liquid polymer.
  • the alkaline agent comprises LiOH, NaOH, KOH, CsOH, RbOH, or combinations thereof.
  • the alkaline agent comprises LiOH, NaOH, KOH, or combinations thereof.
  • the alkaline agent comprises KOH.
  • the electrolyte of the present invention comprises a liquid polymer of formula (I) and an alkaline agent comprising LiOH, NaOH, KOH, CsOH, RbOH, or combinations thereof.
  • the electrolyte comprises a liquid polymer comprising a polyethylene oxide; and an alkaline agent comprising LiOH, NaOH, KOH, CsOH, RbOH, or combinations thereof.
  • the electrolyte comprises a polymer comprising a polyethylene oxide and an alkaline agent comprising KOH.
  • the electrolyte of the present invention comprises more than about 1 wt % of alkaline agent (e.g., more than about 5 wt % of alkaline agent, or from about S wt % to about 76 wt % of alkaline agent).
  • the electrolyte comprises a liquid polymer comprising a polyethylene oxide and 3 wt % or more (e.g., 4 wt % or more, from about 4 wt % to about 33 wt %, or from about 5 wt % to about IS wt %) of an alkaline agent
  • the electrolyte comprises polyethylene oxide and 5 , wt % or more of KOH.
  • the electrolyte consists essentially of a polyethylene oxide having a molecular weight or mean molecular weight from about 100 amu to about 1000 amu and S wt % or more of KOH.
  • Electrolytes useful in the present invention can be substantially free of water.
  • the electrolyte comprises water in an amount of about 60 % of the wt of the alkaline agent or less (e.g., about SO % of the wt of the alkaline agent or less, about 40 % of the wt of the alkaline agent or less, about 30 % of the wt of the alkaline agent or less, about 25 % of the wt of the alkaline agent or less, about 20 % of the wt of the alkaline agent or less, or about 10 % of the wt of the alkaline agent or less).
  • Exemplary alkaline polymer electrolytes include, without limitation, 90 wt % PEG- 200 and 10 wt % KOH, SO wt % PEG-200 and 50 wt % KOH; PEG-dimethyl ether that is saturated with KOH; PEG-dimethyl ether and 33 wt % KOH; PEG-dimethyl ether and 11 wt % KOH; and PEG-dimethyl ether (mean molecular weight of 500 amu) and 33 wt % KOH, that is further diluted to 11 wt % KOH with PEG-dimethyl ether having a mean molecular weight of 200 amu.
  • electrolytes of the present invention can also comprise less than about 10 wt% by weight of electrolyte (e.g., less than about 5 wt% by weight of electrolyte or less than about 1 wt% by weight of electrolyte) of a small carbon chain alcohol such as methanol, ethanol, isopropanol, or mixtures thereof.
  • electrolyte e.g., less than about 5 wt% by weight of electrolyte or less than about 1 wt% by weight of electrolyte
  • a small carbon chain alcohol such as methanol, ethanol, isopropanol, or mixtures thereof.
  • the electrolyte is aqueous KOH, For instance 8M KOH, 12M
  • the electrolyte is aqueous NaOH.
  • Cells of the present invention can include any suitable housing such that the housing does not substantially impede electrical access to the terminals of the cell,
  • the cell housing comprises flexible packaging material
  • the flexible packaging material is used in a sachet configuration or a drawn cavity configuration. Unlike traditional applications of flexible packaging battery packaging requires feed through to carry the current from the enclosed electrochemical cell. Insulating and sealing these feed- throughs can be done by a number of methods, Typical, the flexible packaging material consists of three functional layers, which can be embodied in three physical layer or less (e.g., in some packaging materials, the physical layers perform one, two, or three of the functions performed by functional layers).
  • the first functional layer is an electrolyte compatible layer, This layer provides chemical resistance and physical containment of the liquid or gelatinous electrolyte. Typically this layer can consist of a polyolefm or polyethyl vinyl alcohol that may be co-extruded or mixed with an adhesion promoter, ethyl acrylic acid for example, to facilitate heat sealing or current feed-through adhesion.
  • the second functional layer is a vapor barrier layer. This layer can be a metal, aluminum, or a low transmissibility polymer. This functional layer needs to retard the diffusion of water, electrolyte solvent, oxygen, hydrogen, and carbon dioxide into the cell.
  • the third functional layer provide a physical integrity layer on the outside of the packaging. It provides much of the packaging materials strength and abrasion resistance.
  • This layer may also provide the physical strength to allow the packaging material to be formed into blisters.
  • This layer is typically nylon or mylar in its composition.
  • the functional layer materials can also be applied as conformal coatings to the cells by dip coating or spraying. Cells packaged in flexible packaging typically contain a reduced pressure atmosphere with the absolute pressure inside less than ambient pressure. [00019I] V. EXAMPLES:
  • Example No. 1 Undoped AgO Cathode For Use as Experimental Control A
  • the following material and methods were used to generate undoped AgO cathode material that was used in cells for purposes of generating comparative data concerning cell performance characteristics, i.e., cell cycle life.
  • the undoped AgO cathode material generated using the methods of example no. 1 serves as a control for comparison purposes.
  • Silver nitrate A.C.S. grade, DFG
  • Gelatin from bovine skin, type B, ⁇ 225 bloom, Sigma
  • Potassium hydroxide solution KOH solution, 1.4g/ml, LabChem., Inc.
  • a 2L Aceglass reactor was placed into a hot water bath and a Teflon-coated radial propeller was used. 116.7 g of AgN ⁇ 3 and 1000 g of DI water were added to the reactor and stirred at 400 rpm. The mixture in the reactor was heated to 55 0 C. 0.11 g gelatin was added. In a plastic container, 240 g of KOH solution (1.4g/ml) was mixed with 240 g Dl water to give a diluted KOH solution. The diluted KOH solution was added to the reactor per pump at 55 0 C. At 65 0 C, 198 g of potassium persulfate was added and the temperature was maintained for 50 min.
  • the water was decanted as the solution cooled down and the particles settled.
  • the particles were rinsed with DI water, and once the particles settled, the water was decanted.
  • the particles underwent this rinse and decant process until the ion conductivity of the mixture measured below 25 micro-Ohm.
  • the product was filtered and dried in a 60 0 C vacuum oven.
  • the resultant undoped AgO cathode material is characterized below in Table 1.
  • Particle size analysis was performed using a Horiba LA-930. Diameters on 10%, 50%, and 95% (DlO, D50, and D95) were measured for the samples provided above and below.
  • the resistivities of this cathode material was measured using the following procedure: 3 grams of sample material was loaded into a powder compression cell with a 3,88 cm 2 electrode surface area. Force was applied to the sample from 10 to 40 tons by using a laboratory hydraulic press. The resistance was recorded every 5 tons and the thickness of the sample at 40 tons is also recorded. The resistivity of the sample is the resistance value extrapolated to infinite force divided by final material thickness and multiplied by the area of the powder cell electrodes.
  • Example No. 2 Exemplary In-Doped Cathodes of the Present Invention
  • a 4000 ml Erlenmeyer flask was placed into a hot water bath and a Teflon-coated radial propeller was used for stirring. 301.5 g of AgNC ⁇ and 2500 g of DI water were added to the reaction flask and stirred at 300 rpm. 2.85 g Indium (ID) Nitrate Pentahydrate was dissolved in 100 g DI water and added to the flask. The mixture in the flask was heated to 50 0 C.
  • Table 2 Exemplary cathodes of the present invention comprising indium dopant.
  • Example No. 3 Pb-coated AgO Cathode For Use as Experimental Control B
  • 2.6 wt% lead acetate trihydrate solution was slowly added to a 20 wt% suspension of AgO in de-ionized water.
  • the resulting suspension was allowed to settle, and the water was decanted.
  • the residue was re re-suspend with de-ionized water and decanted.
  • This decanting process was repeated several times and then filtered.
  • the filtrate was dried in vacuum oven at 60 0 C. This process was used to generate standard process yields of about 100 g of Pb-coated AgO, which was used as a test cathode material for evaluating properties of the cathode materials described in Example 1, above.
  • Example No.4 Evaluation of Exemplary Cathode Materials of Example No.2
  • a cathodes prepared in Example No. 2 was employed in an electrochemical cell, depicted in FIGURE 1, to evaluate the effect of the dopant on a cell's cycle life.
  • the cell's cycle life was ascertained by repeatedly cycling the cell attendant to a charge - discharge algorithm wherein the freshly prepared cell, having a 100% SOC equal to about 100% of its rated capacity, is discharged to about 100% of its depth of discharge, i.e., discharged to about 100% DOD, and then re-charged to about 100% SOC, wherein it is again discharged to about 100% DOD.
  • the actual capacity of the cell i.e., the cell's capacity at 100% SOC
  • Figure 2 presents a partial plot of one such evaluation. Using plots of this type, the number of charge cycles at which the cell's actual capacity was observed to be about 70%, about 80%, about 90%, or the like, of the cell's rated capacity can be observed. In conducting these evaluations, tests cells were constructed as described below.
  • Test cells were constructed, as depicted in FIGURE 1, using cathodes incorporating the exemplary cathode material described in Example No, 2 and comparative cells, e.g., control cells, were constructed including a cathode that included the cathode material described in Example No. 3 in one comparative cell and cathode material described in Example No. 1 in a second comparative cell.
  • Each of the cells were constructed from the following materials:
  • Anode Active Material was formulated from 81.9 % Zinc, 5 % PTFE binder
  • Anode Current Coilector in/brass 32 (80/20), 43 mm x 31 mm, pressed at 2T, a commercial product of Dexmet.
  • Anode Adsorber Wrap Solupor (commercially available from Lydall, Inc. of
  • Cathode Active material was formulated from 3% PTFE binder (DuPont TE3859) and cathode material from Example Nos. 1, 2, or 3, depending on the cell, to give a filial mass of 5.85 g.
  • Cathode Current Collector silver, commercial product of Dexm ⁇ t. Cathode was pressed at 5.5T.
  • Electrode Separators 2 adjacent separators were employed wherein one separator was formed from Innovia 32(80/20) soaked with 1 ml electrolyte and the second separator was formed from Innovia 32(80/20) (separator materials are commercially available from
  • Electrolyte 32% by weight aqueous KOH and NaOH mixture (80/20 mol ratio)
  • Table 3 Results of charge-discharge cycle testing for In-doped AgO cathodes.
  • Table 4 Results of charge-discharge cycle testing for Pb-coated AgO cathode.
  • FIGURE 2 presents the charge profiles for the test cells including the Pb-Coated AgO test cathode material and 2.0 wt% In doped AgO cathode material for comparison.
  • Example No. 5 Exemplary AI-Doped Cathodes of the Present Invention
  • a 4000 ml Erlenmeyer flask was placed into a hot water bath and a Teflon-coated radial propeller was used for stirring. 301.5 g of AgNOa and 2500 g of DI water were added to the reaction flask and stirred at 300 rpm. 2.85 g aluminum hydroxide was dissolved in 100 g DI water and added to the flask.
  • Silver nitrate A.C.S. grade, DFG
  • Gallium (III) nitrate hydrate 99.9% metals basis, Aldrich
  • Potassium hydroxide solution KOH solution, 1.4g/ml, LabChem., Inc.
  • a 2L Aceglass reactor was placed into a hot water bath and a Teflon-coated radial propeller was used.
  • 116.7 g of AgNO 3 and 1000 g of DI water were added to the reactor and stirred at 400 rpm.
  • 0.77 g Gallium (EU) nitrate hydrate was dissolved in 100 g DI water and added to the reactor.
  • the mixture in the reactor was heated to 55 0 C.
  • 0.11 g gelatin was added.
  • 240 g of KOH solution (1.4 g/ml) was mixed with 240 g DI water to give a diluted KOH solution.
  • the diluted KOH solution was added to the reactor per pump at 55 0 C.
  • the mixture was heated to 65 0 C, 198 g of potassium persulfate was added, and the temperature was maintained for 50 min.
  • the water was decanted as the solution cooled down, and the particles settled.
  • the particles were rinsed with DI water, and once the particles settled, the water was decanted.
  • the particles underwent this rinse and decant process until the ion conductivity of the mixture measured below 25 micro-Ohm.
  • the product was filtered and dried in a vacuum oven at 60 0 C.
  • Example No.7 Evaluation of Exemplary Cathode Materials of Example No.6
  • Test cells and comparative cells were constructed and evaluated as described above in Example No.4 and FIGURE 1, wherein the test cell was formulated as described above, substituting the cathode material of Example No. 6 for the cathode material of Example No. 2 in the test cell, and employing a comparative cell described above using a cathode material of Example No. 1.
  • the life cycle data comparison of test cell incorporating Ga-doped cathode material of Example No.6 and the comparative cathode incorporating the cathode material of Example No. 1 is presented in Table 6:
  • Example No. 8 Exemplary 1.3% B-Doped Cathodes of the Present Invention
  • Silver nitrate A.C.S. grade, DFG
  • Gelatin from bovine skin, type 6, -225 bloom, Sigma
  • Potassium hydroxide solution KOH solution, 1.4g/ml, LabChem., Inc.
  • a 2L Aceglass reactor was placed into a hot water bath and a Teflon-coated radial propeller was used.
  • 116.7 g of AgNO 3 and 1000 g of DI water were added to the reactor and stirred at 400 rpm.
  • 1.11 g Boron oxide was dissolved in 100 g DI water and added to the reactor.
  • the mixture in the reactor was heated to 55 0 C. 0.11 g gelatin was added.
  • 240 g of KOH solution (1.4g/ral) was mixed with 240 g DI water to give a diluted KOH solution.
  • the diluted KOH solution was added to the reactor per pump at 55 0 C.
  • 198 g of potassium persulfate was added, and add the temperature was maintained for 50 min.
  • Table 7 Exemplary cathode of the present invention comprising boron dopant.
  • Silver nitrate A.C.S. grade, DFG
  • Gelatin from bovine skin, type B, -225 bloom, Sigma
  • Potassium hydroxide solution KOH solution, 1.4g/ml, LabChem., Inc.
  • a 2L Aceglass reactor was placed into a hot water bath and a Teflon-coated radial propeller was used. 116,7 g of AgNO 3 and 1000 g of DI water were added to the reactor and stirred at 400 rpm. 3.06 g Ytterbium (111) nitrate pentahydrate was dissolved in 100 g Dl water and added to the reactor. The mixture in the reactor was heated to 55 0 C. 0.11 g gelatin was added.
  • Example No. 10 Evaluation of Exemplary Cathode Materials of Example No. 8
  • Test cells were constructed and evaluated as described above in Example Nos.4 and 7 wherein the test cells were formulated as described above, substituting the cathode material of Example No. 8 in the test cell or Example No. 1 in the comparative cell.
  • the life cycle data comparison of test cell incorporating B-doped cathode material of Example No. 8 and the comparative cathode incorporating the cathode material of Example No. 1 is presented in Table 8:

Abstract

The present invention provides novel cathodes having a reduced resistivity and other improved electrical properties. Furthermore, this invention also presents methods of manufacturing novel electrochemical cells and novel cathodes. These novel cathodes comprise a silver material that is doped with a Irivalent species.

Description

IMPROVED CATHODE
CROSS REFERENCE TO RELATED APPLICATIONS
This PCT application claims priority to U.S. Application No. 61/164,080, filed on March 27, 2009, and U.S. Application No, 61/164,216, filed on March 27, 2009. The entire contents of the aforementioned applications are incorporated herein by reference in their entireties.
This invention is concerned with a new cathode formed by doping a cathode material with a dopant that imparts the cathode with one or more improved properties over traditional cathodes.
When a traditional battery is discharged, the anode supplies positive ions to an electrolyte and electrons to an external circuit. The cathode is typically an electronically conducting host into which positive ions are inserted reversibly from the electrolyte as a guest species and are charge-compensated by electrons from the external circuit. A secondary battery, or cell, uses a reaction that can be reversed when current is applied to the battery, thus '"recharging" the battery. The chemical reactions at the anode and cathode of a secondary battery must be reversible. On charge, the removal of electrons from the cathode by an external field releases positive ions back to the electrolyte to restore the parent host structure, and the addition of electrons to the anode by the external field attracts charge- compensating positive ions back into the anode to restore it to its original composition. [0004] Traditional electrode materials such as cathode active materials suffer a number of drawbacks. For instance, many traditional cathodes possess art elevated impedance or internal resistance that negatively effects battery discharge, and thus, restricts battery performance. As many traditional batteries progress through charge cycles, the deleterious effect of impedance causes an increased hindrance on battery performance. [0005] Thus, there is a need for electrode materials that have improved properties and can improve battery performance.
SUMMARY OF THE INVENTION
[0006] One aspect of the present invention provides a cathode for use in an electrochemical cell comprising a silver material that is doped with a trivalent dopant to give a doped silver material, wherein the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the cathode. In some embodiments of this aspect, the cathode further comprises from about 0.5 wt% to about S wt% of bivalent dopant In other embodiments of this aspect, the cathode further comprises from about 1 wt% to about 8 wt% of trivalent dopant. In other embodiments, the doped silver material comprises a powder. For example, the doped silver material comprises a powder, and the powder has a mean particle diameter of about 20 μm or less. In another example, the doped silver material comprises a powder, and the powder has a mean particle diameter of about IS μm or less. Ih other examples, the powder has a mean particle diameter of about 5 μm or less. In some embodiments, the silver material comprises Ag, AgO, Ag2O, Ag2O3, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, or any combination thereof. Some cathodes of this aspect further comprise a binder. For example, the cathode further comprises a binder, and the binder comprises FTFE or PVDF. hi other embodiments of this aspect, the dopant comprises at least one Group 13 element. For example, the dopant comprises aluminum, indium, gallium, boron, thallium, or any combination thereof, hi other examples, the dopant comprises aluminum, indium, gallium, boron, or any combination thereof, hi some embodiments, the dopant comprises a lanthanide element. For example, the lanthanide element is Yb. [0007] Another aspect of the present invention provides a cathode for use in an electrochemical cell comprising a doped silver material comprising a dopant, wherein the dopant comprises gallium, boron, or a combination thereof, and the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the cathode, hi some embodiments of this aspect, the cathode comprises from about 0.5 wt% to about 5 wt% of dopant In some embodiments of this aspect, the cathode comprises from about 1 wt% to about 8 wt% of dopant In other embodiments, the doped silver material of the cathode comprises a powder. For example, the doped silver material comprises a powder, and the powder has a mean particle diameter of about 20 μm or less. In other examples, the doped silver material comprises a powder, and the powder has a mean particle diameter of about 15 μm or less, hi another example, the powder has a mean particle diameter of about 5 μm or less, hi some embodiments of this aspect, the silver material comprises Ag, AgO, Ag2O, Ag2O3, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, or any combination thereof. Other cathodes of this aspect further comprise a binder. For example, the cathode further comprises a binder, and the binder comprises PTFE or PVDF. hi other embodiments of this aspect, the dopant comprises gallium. And, in some embodiments, the dopant comprises boron. In some embodiments, the dopant comprises a lanthanide element. For example, the lanthanide element is Yb. [0008] Another aspect of the present invention provides a cathode for use in an electrochemical cell comprising a doped silver material comprising a dopant, wherein the dopant comprises indium, aluminum, or a combination thereof, and the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the cathode. In some embodiments of this aspect, the cathode further comprises from about 0.S wt% to about S wt% of dopant. In some embodiments of this aspect, the cathode further comprises from about 1 wt% to about S wt% of dopant. In other embodiments, the doped silver material comprises a powder. For example, the doped silver material comprises a powder, and the powder has a mean particle diameter of about 20 urn or less. In other examples, the doped silver material comprises a powder, and the powder has a mean particle diameter of about 15 μm or less. In another example, the powder has a mean particle diameter of about 5 μm or less. In another embodiment of this aspect, the doped silver material comprises Ag, AgO, Ag2O, Ag2O3, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, or any combination thereof . Some cathodes of this aspect further comprise a binder. For example, the cathode further comprises a binder, and the binder comprises PTFE or PVDF. In some embodiments of this aspect, the dopant comprises indium. In others, the dopant comprises aluminum.
[0009] Another aspect of the present invention provides a method of producing a cathode for use in an electrochemical cell comprising providing a silver powder that is doped with from about 0.25 wt% to about 10 wt% of a trivalent dopant by weight of the cathode to give a doped silver powder; and forming the doped silver powder into a cathode. In some methods, the doped silver powder is doped with from about 0.5 wt% to about 5 wt% of dopant In some methods, the doped silver powder is doped with from about 1 wt% to about 8 wt% of dopant In other methods, the doped silver powder has a mean particle diameter of about 20 μm or less, hi some methods, the doped silver powder has a mean particle diameter of about 15 μm or less. For example, the doped silver powder has a mean particle diameter of about 5 μm or less. In other methods, the doped silver powder comprises Ag, AgO, Ag2O, Ag2O3, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, or any combination thereof. For example, the doped silver powder comprises AgO, Ag2O, Ag2O3, or any combination thereof. Some methods further comprise the step of providing a binder. For example, the method further comprises providing a binder, wherein the binder comprises PTFE or PVDF. hi some methods, the dopant comprises a lanthanide. For example, the dopant comprises Yb. In other methods, the dopant comprises at least one Group 13 element. For example, the dopant comprises gallium, boron, indium, aluminum, thallium, or any combination thereof. In other examples, the dopant comprises gallium, boron, or a combination thereof. And in some methods, the dopant comprises indium, aluminum, or a combination thereof.
[00010] Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein the dopant comprises a trivalent dopant, and the dopant is present in a sufficient concentration to impart the cell with at least 70% (e.g., at least 80%, at least 85%, or at least 90%) capacity over at least 100 cycles (e.g., at least 150 cycles, at least 120 cycles, at least 200 cycles, at least 250 cycles, at least 300 cycles, at least 320 cycles, at least 350 cycles, or at least 400), In some embodiments, the present invention provides an electrochemical cell comprising a cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein the dopant comprises a trivalent dopant, and the dopant is present in a sufficient concentration to impart the cell with about 80% or greater (e.g., at least 85%, at least 85%, or at least 90%) capacity over at least 120 cycles (e.g., at least 150 cycles, at least 200 cycles, at least 250 cycles, at least 300 cycles, at least 350 cycles, or at least 400 cycles). In some embodiments, the present invention provides an electrochemical cell comprising & cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein the dopant comprises a trivalent dopant, and the dopant is present in a sufficient concentration to impart the cell with about 80% or greater (e.g., at least 85%, at least 85%, or at least 90%) capacity over at least 150 cycles. In some embodiments of this aspect, the silver material comprises from about 0.25 wt% to about 10 wt% of trivalent dopant. In some embodiments of this aspect, the silver material comprises from about 0.5 wt% to about 5wt% of trivalent dopant. In other embodiments, the silver material comprises a powder. For example, the silver material comprises a powder, and the powder has a mean particle diameter of about 20 μm or less, In other examples, the silver material comprises a powder, and the powder has a mean particle diameter of about 15 μm or less. In other examples, the powder has a mean particle diameter of about 5 μm or less. In some embodiments, the cathode, the anode, or both further comprises a binder, In some embodiments, the cathode further comprises a binder. For instance, the cathode comprises a binder, and the binder comprises PTFE or PVDF. In other embodiments, the anode further comprises a binder. For instance, the anode further comprises a binder, and the binder comprises PTFE or PVDF. Several other embodiments further comprise an electrolyte comprising NaOH, KOH, or a combination thereof. In some embodiments, the silver powder comprises Ag, AgO, Ag2O, Ag2O3, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, or any combination thereof. For example, the silver powder comprises AgO, Ag2O, Ag2O3, or any combination thereof. In other examples, the silver material comprises AgO. And, in another example, the silver material comprises Ag2O. Ih several embodiments, the dopant comprises at least one Group 13 element. For example, the dopant comprises indium, aluminum, gallium, boron, thallium, or any combination thereof. In other examples, the dopant comprises indium, aluminum, or a combination thereof. And in some examples, the dopant comprises gallium, boron, or a combination thereof. In some embodiments, the dopant comprises a lanthanide element. For example, the lanthanide element is Yb.
[00011] Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising silver powder comprising from about 0.25 wt% to about 10 wt% of a trivalent dopant; an anode comprising zinc; and an electrolyte comprising KOH. For example, the silver powder has a mean particle diameter of about IS μm or less. Ih other examples, the powder has a mean particle diameter of about S μm or less. In some embodiments, the cathode, the anode, or both comprise a binder. For example, the cathode comprises a binder. Ih some instances, the cathode comprises a binder, and the binder comprises PTFE or FVDF. In other examples, the anode comprises a binder. For instance, the anode comprises a binder, and the binder comprises PTFE or PVDF. Other embodiments further comprise an electrolyte comprising NaOH, KOH, or a combination thereof. In some embodiments, the silver powder comprises Ag, AgO, Ag2O, Ag2Oa, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, or any combination thereof. For example, the silver powder comprises AgO, Ag2O, Ag2Os, or any combination thereof. In other examples, the silver material comprises AgO. And in some examples, the silver material comprises Ag2O. In some embodiments, the dopant comprises at least one Group 13 element. For example, the dopant comprises indium, aluminum, gallium, boron, thallium, or any combination thereof. Or, the dopant comprises indium, aluminum, or a combination thereof. In other examples, the dopant comprises gallium, boron, or a combination thereof. [00012] Another aspect of the present invention provides a cathode for use in an electrochemical cell comprising a doped silver material comprising a dopant, wherein the dopant comprises a lanthanide element, aluminum, indium, gallium, boron, or a combination thereof, and the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the doped silver material. In several embodiments, the lanthanide element comprises Yb. BRIEF DESCRIPTION OF THE FICTIUKS
[00013] FIGURE 1 is an exploded view of an exemplary electrochemical cell of the present invention that was employed in cell cycle testing described in Example Nos. 4 and 7; [00014] FIGURE 2 is a graphical plot of charge-discharge testing for an exemplary electrochemical cell of the present invention, which is superimposed on a graphical representation of charge-discharge testing results for a control electrochemical test cell; and [00015] FIGURE 3 is a graphical plot of the actual capacity of an exemplary cell of the present invention as a function of cycle number.
[00016] These figures are demonstrative of exemplary embodiments of the present invention and are not intended to limit its scope.
DETAILED DESCRIPTION
[00017] The present invention provides cathodes, methods of making cathodes, and electrochemical cells (e.g., batteries) that employ these cathodes having improved properties over traditional cathodes, methods, or electrochemical cells. [00018] I. DEFINITIONS
[00019] As used herein, the term "battery" encompasses electrical storage devices comprising one electrochemical cell or a plurality of electrochemical cells. A "secondary battery" is rechargeable, whereas a "primary battery" is not rechargeable. For secondary batteries of the present invention, a battery anode is designated as the positive electrode during discharge, and as the negative electrode during charge. [00020] As used herein, the terms "silver material" or "silver powder" refer to any silver compound such as Ag, AgO, Ag2O, Ag2O3, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, hydrates thereof, or any combination thereof. Note that "hydrates' of silver include hydroxides of silver. Because it is believed that the coordination sphere surrounding a silver atom is dynamic during charging and discharging of the cell wherein the silver serves as a cathode, or when the oxidation state of the silver atom is in a state of flux, it is intended that the term 'silver* or 'silver material' encompass any of these silver oxides and hydrates (e.g., hydroxides). Terms 'silver' or 'silver material1 also includes any of the abovementioned species that are doped and/or coated with dopants and/or coatings that enhance one or more properties of the silver. Exemplary dopants and coatings are provided below. In some examples, silver or silver material includes a silver oxide further comprising an indium or aluminum dopant or coating, m some examples, silver or silver material includes a silver oxide further comprising Group 13 elements. In some examples, silver or silver material includes a silver oxide further comprising a bivalent dopant. Note that the term "oxide" used herein does not, in each instance, describe the number of oxygen atoms present in the silver or silver material. For example, a silver oxide may have a chemical formula of AgO, Ag2Os, or a combination thereof. Furthermore, silver can comprise a bulk material or silver can comprise a powder having any suitable mean particle diameter. [00021] As used herein, "iron oxide" refers to any oxide or hydroxide of iron, e.g., FeO, Fe2O3, Fe3O4, or any combination thereof.
[00022] As used herein, "boron oxide" refers to any oxide or hydroxide of boron, e.g., B2O3. [00023] As used herein, "aluminum oxide" refers to any oxide or hydroxide of aluminum, e.g., Al2O3.
[00024] As used herein, "gallium oxide" refers to any oxide or hydroxide of gallium, e.g., Ga2O3.
[00025] As used herein, "indium oxide" refers to any oxide or hydroxide of indium, e.g., In2O3.
[00026] As used herein, "thalium oxide" refers to any oxide or hydroxide of thalium, e.g., Th2O3.
[00027] As used herein, "Group 13 elements" refers to one or more of the chemical elements classified in the periodic table of elements under column number 13. These elements include boron, aluminum, gallium, indium, thallium, and ununtrium. [00028] As used herein, "trivalent dopant" refers to an element or polyatomic species that substantially exists in the 3+ oxidation state when combined (e.g., doped) with a silver material. Examples of trivalent dopants include Group 13 elements, lanthanides (e.g., Yb), and polyatomic species having a +3 oxidation state. [00029] As used herein, the terms "divalent silver oxide" and "AgO" are used interchangeably.
[00030] As used herein, the term "alkaline battery" refers to a primary battery or a secondary battery, wherein the primary or secondary battery comprises an alkaline electrolyte.
[00031] As used herein, "lanthanide" refers to elements in a series that comprise the fourteen elements with atomic numbers 58 through 71, from cerium to lutetium. AU lanthanides are f-block elements, corresponding to the filling of the 4f electron shell. Lanthanum, which is a d-block element, may also be considered to be a lanthanide. All lanthanide elements form trivalent cations, Ln3+, whose chemistry is largely determined by the ionic radius, which decreases steadily for lanthanum to lutetium. Examples of lanthanides include Lanthanum (La), Cerium (Ce), Praseodymium (Pr), Neodymium (Nd), Promεthium (Pm), Samarium (Sm), Europium (Eu), Gadolinium (Gd), Terbium (Tb), Dysprosium (Dy). Holmium (Ho), Erbium (Er), Thulium (Tm), Ytterbium (Yb), or Lutεtium (Lu).
[00032] As used herein, a "dopant" or "doping agent" refers io a chemical compound thai is added io a substance in low concentrations in order to alter the optical/electrical properties of the semiconductor. For example, a dopant may be added to the powder active material of a cathode to improve its electronic properties (e.g., reduce its impedance and/or resistivity or improve a cell's cycle life where the cathode, is employed in said cell). In other examples, doping occurs when one or more atoms of a crystal lattice of a bulk material is substituted with one or more atoms of a dopant,
[00033] As used herein, an "electrolyte" refers to a substance that behaves as an electrically conductive medium. For example, the electrolyte facilitates the mobilization of electrons and cations in the cell. Electrolytes include mixtures of materials such as aqueous solutions of alkaline agents. Some electrolytes also comprise additives such as buffers. For example, an electrolyte comprises a buffer comprising a borate or a phosphate. Exemplary electrolytes include, without limitation, aqueous KOH, aqueous NaOH, a mixture of aqueous NaOH and KOH, or the liquid mixture of KOH, NaOH, or a combination thereof in a polymer. [00034] As used herein, "alkaline agent" refers to a base or ionic salt of an alkali metal (e.g., an aqueous hydroxide of an alkali metal). Furthermore, an alkaline agent forms hydroxide ions when dissolved in water or other polar solvents. Exemplary alkaline electrolytes include without limitation LiOH, NaOH, KOH, CsOH, RbOH, or combinations thereof. Electrolytes can optionally include other salts to modify the total ionic strength of the electrolyte, for example KF or Ca(OH)2-
[0003S] A "cycle" or ''charge cycle" refers to a consecutive charge and discharge of a cell or a consecutive discharge and charge of a cell. For example, a cell undergoes one cycle when, freshly prepared, it is discharged of about 100% of its DOD and re-charged to about 100% of its SOC, In another example, a freshly prepared cell undergoes 2 cycles when the cell is:
1) Cycle 1 : discharged of about 100% of its DOD and re-charged to about 100% SOC; immediately followed by
2) Cycle 2: a second discharge of about 100% of its DOD and re-charged to about 100% SOC.
[00036] It is noted that this process may be repeated to subject a cell to as many cycles as is desired or practical [00037] As used herein, "Ah" refers to Ampere (Amp) Hour and is a scientific unit denoting the capacity of a battery or electrochemical cell A derivative unit, "'mAh" represents a milliamp hour and is 1/1000 of an Ah.
[0CI038] As used herein, "depth of discharge" and "DOD" are used interchangeably to refer to the measure of how much energy has been withdrawn from a battery or cell, often expressed as a percentage of capacity, e.g., rated capacity. For example, a 100 Ah battery from which 30 Ah has been withdrawn has undergone a 30% depth of discharge (DOD). [00039] As used herein, "state of charge'' and "SOC" and used interchangeably to refer to the available capacity remaining in a battery, expressed as a percentage of the cell or battery's rated capacity.
[0004Oj For convenience, the polymer name "polyvinylidenε fluoride" and its corresponding initials "PVDF" are used interchangeably as adjectives to distinguish polymers, solutions for preparing polymers, and polymer coatings, Use of these names and initials in no way implies the absence of other constituents. These adjectives also encompass substituted and co- polyraerized polymers, A substituted polymer denotes one for which a substituent group, a methyl group, for example, replaces a hydrogen or fluorine on the polymer backbone. [OCMMIj For convenience, the polymer name "polytetrafluoroethylene" and its corresponding initials 'TTFE1' are used interchangeably as adjectives to distinguish polymers, solutions for preparing polymers, and polymer coatings. Use of these names and initials in no way implies the absence of other constituents. These adjectives also encompass substituted and co- polynierized polymers. A substituted polymer denotes one for which a substituent group, a methyl group, for example, replaces a hydrogen on the polymer backbone. [00042] As used herein, "organometallic complex" and "complex" refer to complexes or compounds having bonds or binding interactions (e.g., electrostatic interactions) between a metal (e.g., lead) and one or more organic ligands (e.g,, nitrate or acetate). The organic ligands often bind the metal through a heteroatom such as oxygen or nitrogen. [00043] Batteries and battery electrodes are denoted with respect to the active materials in the fully-charged state. For example, a zinc-silver battery comprises an anode comprising zinc and a cathode comprising a silver powder (e.g., Ag2Q3), Nonetheless, more than one species is present at a battery electrode under most conditions. For example, a zinc electrode generally comprises zinc metal and zinc oxide (except when fully charged), and a silver powder electrode usually comprises AgO, Ag2U3 and/or Ag2θ and silver metal (except when MIy discharged). [00044] As used herein, "maximum voltage" or "rated voltage" refers to the maximum voltage an electrochemical cell can be charged without interfering with the cell's intended utility. For example, in several zinc-silver electrochemical cells that are useful in portable electronic devices, the maximum voltage is less than about , about 2.3 V or less, or about 2.0 V). In other batteries, such as lithium ion batteries that are useful in portable electronic devices, the maximum voltage is less than about 15.0 V (e.g., less than about 13.0 V, or about 12.6 V or less). The maximum voltage for a battery can vary depending on the number of charge cycles constituting the battery's useful life, the shelf-life of the battery, the power demands of the battery, the configuration of the electrodes in the battery, and the amount of active materials used in the battery.
[00045] As used herein, an "anode" is an electrode through which (positive) electric current flows into a polarized electrical device. In a battery or galvanic cell, the anode is the negative electrode from which electrons flow during the discharging phase in the battery. The anode is also the electrode that undergoes chemical oxidation during the discharging phase. However, in secondary, or rechargeable, cells, the anode is (he electrode that undergoes chemical reduction during the cell's charging phase. Anodes are formed from electrically conductive or semiconductive materials, e.g., metals, metal oxides, metal alloys, metal composites, semiconductors, or the like. Common anode materials include Si, Sn, Al, Ti, Mg, Fe, Bi, Zn, Sb, Ni, Pb, Li, Zr, Hg, Cd, Cu, LiC6, mischmetals, alloys thereof, oxides thereof, or composites thereof. Anode materials such as zinc may even be sintered. [00046] Anodes may have many configurations. For example, an anode may be configured from a conductive mesh or grid that is coated with one or more anode materials. Li another example, an anode may be a solid sheet or bar of anode material. [00047] As used herein, a "cathode" is an electrode from which (positive) electric current flows out of a polarized electrical device. In a battery or galvanic cell, the cathode is the positive electrode into which electrons flow during the discharging phase in the battery. The cathode is also the electrode that undergoes chemical reduction during the discharging phase. However, in secondary or rechargeable cells, the cathode is the electrode that undergoes chemical oxidation during the cell's charging phase. Cathodes are formed from electrically conductive or semiconductive materials, e.g., metals, metal oxides, metal alloys, metal composites, semiconductors, or the like. Common cathode materials include Ag, AgO, Ag2O3, Ag2O, HgO, Hg2O, CuO, CdO, NiOOH, Pb2O4, PbO2, IiFePO4, U3V2(PO4J3, V6O13, V2O5, Fe3O4, Fe2O3, MnO2, IiCoO2, LiNiO2, IiMn2O4, or composites thereof. Cathode materials such as Ag, AgO, Ag2O3 may even be sintered. Cathodes may also have many configurations. For example, a cathode may be configured from a conductive mesh that is coated with one or more cathode materials. In another example, a cathode may be a solid sheet or bar of cathode material, [00049] As used herein, the term "electronic device" is any device that is powered by electricity. For example, and electronic device can include a portable computer, a portable music player, a cellular phone, a portable video player, or any device that combines the operational features thereof.
[00050] As used herein, the term "cycle life" is the maximum number of times a secondary battery can be cycled while retaining a capacity useful for the battery's intended use (e.g., the number of times a cell may be cycled until the cell's 100% SOC, i.e., its actual capacity, is less than 90% of its rated capacity (e.g., less than 85% of its rated capacity, about 90% of its rated capacity, or about 80% of its rated capacity), to some instances, 'cycle life' is the number of times a secondary battery or cell can be cycled until the cell's 100% SOC is at least about 60 percent of its rated capacity (e.g., at least about 70 percent of its rated capacity, at least about 80 percent of its rated capacity, at least 90 percent of its rated capacity, at least 95 percent of its rated capacity, about 90% of its rated capacity, or about 80% of its rated capacity).
[00051] As used herein, the symbol "M" denotes molar concentration. [00052] Batteries and battery electrodes are denoted with respect to the active materials in the fully-charged state. For example, a zinc-silver battery comprises an anode comprising zinc and a cathode comprising a silver powder (e.g., AgO or Ag2O3). Nonetheless, more than one species is present at a battery electrode under most conditions. For example, a zinc electrode generally comprises zinc metal and zinc oxide (except when fully charged), and a silver powder electrode usually comprises silver powder (e.g., AgO, Ag2©3 and/or Ag2O and silver metal (except when fully discharged).
[00053] As used herein, the term "oxide" applied to alkaline batteries and alkaline battery electrodes encompasses corresponding "hydroxide" species, which are typically present, at least under some conditions.
[001154] As used herein, the term, "powder" refers to a granular solid composed of a plurality of fine particles. In some instances, a powder's granules may flow freely when shaken or tilted, and in other instances, a powder's granules may cohere together, for example, in powders comprising a binder.
[00055] As used herein, the term, "mean diameter" or "mean particle diameter" refers to the diameter of a sphere that has the same volume/surface area ratio as a particle of interest. As used herein, the terms "substantially stable" or ''substantiaily inert" refer to a compound or component that remains substantially chemically unchanged in the presence of an alkaline electrolyte (e.g., potassium hydroxide) and/or in the presence of an oxidizing agent (e.g., silver ions present in the cathode or dissolved in the electrolyte). [00057] As used herein, "charge profile" refers to a graph of an electrochemical cell's voltage or capacity with time or cycle number. A charge profile can be superimposed on other graphs such as those including data points such as charge cycles or the like, [000581 As used herein, "resistivity" or "impedance" refers to the internal resistance of a cathode in an electrochemical cell. This property is typically expressed in units of Ohms or micro-Ohms.
[Θ0Θ59] As used herein, the terms "first" and/or "second" do not refer to order or denote relative positions in space or time, but these terms are used to distinguish between two different elements or components. For example, a first separator does not necessarily proceed a second separator in time or space; however, the first separator is not the second separator and vice versa. Although it is possible for a first separator to precede a second separator in space or time, it is equally possible that a second separator precedes a first separator in space or time.
[00060] As used herein, the term "nanometer" and "nnV' are used interchangeably and refer to a unit of measure equaling IxIO"9 meters.
As used herein, the term "cathode active material1' or "cathode" refer to a composition that includes silver, as described above (e.g., doped silver, coated silver, silver that is doped or coated, or any combination thereof),
[00062] As used herein, the term "capacity" refers to the mathematical product of a cell's discharge current and the time (in hours) during which the current is discharged until the cell reaches its terminal voltage.
[00063] Similarly, the term "actual capacity" refers to the capacity of the battery or cell when the cell has 100% SOC. In general terms, the capacity of a cell/battery is the amount of charge available expressed in ampere-hours (Ah), An ampere is the urait of measurement used for electrical current and is defined as a coulomb of charge passing through an electrical conductor in one second. The capacity of a cell or battery is related to the quantity of active materials present, the amount of electrolyte present, and the surface area of the electrodes. The capacity of a battery/cell can be measured by discharging at a constant current until it reaches its terminal voltage, which depends on the cell's intended usage. [00064] A cell's "rated capacity" is the capacity that a cell should theoretically discharge at 100% SOC based on the amounts of electrode materials present in the cell, the amount of electrolyte present in the cell, the surface area of the electrodes, and the cell's intended usage. For many types of cells, industry standards establish a cell's rated capacity, which is based on the cell's intended usage. [00065] II. CATHODES
100066] One aspect of the present invention provides a cathode for use in an electrochemical cell comprising a silver material that is doped with a trivaient dopant to give a doped silver material, wherein the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the cathode.
[00067] Another aspect of the present invention provides a cathode for use in an electrochemical cell comprising a silver material that is doped with a dopant comprising at least one Group 13 element to give a doped silver material, wherein the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the cathode, [00068] Another aspect of the present invention provides a cathode for use in an electrochemical cell comprising a silver material that is doped with gallium, thallium, boron, indium, aluminum, or any combination thereof, to give a doped silver material, wherein the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the cathode.
[00069] Another aspect of the present invention provides a cathode for use in an electrochemical cell comprising a silver material that is doped with indium, aluminum, or a combination thereof, to give a doped silver material, wherein the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the cathode. [00070] Another aspect of the present invention provides a cathode for use in an electrochemical eel! comprising a silver material that is doped with gallium, boron, or a combination thereof, to give a doped silver material, wherein the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the cathode. [00071] In some embodiments above, the doped silver material comprises from about 0,5 wt% to about 5 wt% of trivaient dopant. In other embodiments above, the doped silver material comprises from about 1 wt% to about 8 wt% of trivaient dopant. In other embodiments, the silver material of the cathode comprises a powder. For instance, the powder has a mean particle diameter of about 20 μm or less (e.g., 15 μm or less, or 10 μm or less). In other instances, the powder has a mean particle diameter of about 15 μm or less (e.g., 10 μm or less). In other instances, the powder has a mean particle diameter of about 5 μm or less. Li other embodiments, the doped silver material comprises Ag, AgO, AgO, Ag2O3, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, or any combination thereof. In some embodiments, die cathode further comprises a binder. For example, the cathode comprises a binder and the binder comprises PTFE or PVDF. [00072] One aspect of the present invention provides a cathode for use in an electrochemical cell comprising a silver material comprising a dopant, wherein the dopant comprises indium, aluminum, or a combination thereof, and the dopant is present in a sufficient concentration such that cathode has a resistivity of about 500hm*cm or less. In several embodiments, the dopant is present in a sufficient concentration such that cathode has a resistivity of about 40 Ohm'cm or less. In several embodiments, the dopant is present in a sufficient concentration such that cathode has a resistivity of about 35 0hm*cm or less. In several embodiments, the dopant is present in a sufficient concentration such that cathode has a resistivity of about 30 Ohm*cm or less.
[00073] In one embodiment, the cathode comprises from about 0.25 wt% to about 10 wt% of dopant. For example, the cathode comprises from about 0.75 wt% to about 9 wt% of dopant. In other examples, the cathode comprises from about 1 wt% to about 8 wt% of dopant And, in some examples, the cathode comprises from about 0.5 wt% to about 5 wt% of dopant. [00074] Also, cathodes of the present invention comprise a silver material. The silver material includes bulk material that may be doped with a dopant, as provided herein, or the silver material may comprise a powder. In embodiments, where the silver material comprises a powder, the powder may be doped or coated (e.g., a plurality of the granuals of silver material comprising the powder are doped with a dopant). Furthermore, the powder may undergo further processing (e.g., hot pressing, or the like) to generate a silver bulk material that is useful in cathodes of the present invention.
[00075] hi another embodiment, the cathode comprises a silver powder that is doped with a dopant, wherein the doped silver powder has a mean particle diameter of about 15 μm or less. For example, the doped silver powder has a mean particle diameter of about 10 μm or less. In other examples, the doped silver powder has a mean particle diameter of about 7 μm or less. And, in other examples, the doped silver powder has a mean particle diameter of about 5 μm or less.
[0007(Q hi several embodiments, the cathodes comprise silver material (e.g., silver powder) and the silver material comprises Ag, AgO, Ag2O, Ag2Oa, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, hydrates thereof, or any combination thereof. For example, the cathode comprises silver material (e.g., silver powder), which comprises AgO.
In another example, the silver powder comprises Ag2Oa.
[00077] Cathodes of the present invention can optionally comprise additives such as binders, or other additives to improve one or more features of the cathode. In one example, the cathode comprises a binder. Suitable binders include any binder that is substantially inert to the silver oxide powder or doped silver oxide powder. For example, the binder comprises
PTFE or PVDF.
[00078] In another embodiment, a cathode for use in an electrochemical cell comprising a silver powder doped with a sufficient concentration of indium such that cathode has a resistivity of about 30 Ohm»cm or less; and the doped silver powder has a mean particle diameter of about 7 μm or less.
[00079] In another embodiment, a cathode for use in an electrochemical cell comprising a silver powder doped with a sufficient concentration of aluminum such that cathode has a resistivity of about 30 Ohm»cm or less; and the doped silver powder has a mean particle diameter of about 7 μm or less.
[00080] In another embodiment, a cathode comprises a silver powder that is doped with a sufficient amount of aluminum, indium, or a combination thereof to provide a resistivity of about 30 Ohm'cm or less and has a mean particle diameter of about 7 μm or less, wherein the silver powder comprises Ag, AgO, Ag2O, Ag2Qs, AgOH, AgOOH, AgONa, AgCuO2,
AgFeO2, AgMnO2, Ag(OH)2, hydrates thereof, or any combination thereof.
[00081] As noted above, cathodes of the present invention can optionally comprise additives such as binders, current collectors, or the like. Ih several examples, the cathode of the present invention comprises a binder. For instance, the cathode comprises a binder, and the binder comprises PTFE, PVDF (e.g.f PVDF-co-HFP), CMC, PVP, PAA, or a copolymer thereof.
[00082] Furthermore cathodes of the present invention comprise silver powder. Silver powder includes Ag, AgO, Ag2O, Ag2Oj, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2,
AgMnO2, Ag(OH)2, hydrates thereof, or any combination thereof.
[00083] Another aspect of the present invention provides a cathode for use in an electrochemical cell comprising a silver powder comprising a dopant, wherein the dopant comprises aluminum, and the dopant is present in a sufficient concentration such that cathode has a resistivity of about 40 Ohnrem or less.
[00084] Ih one embodiment, the cathode comprises from about 0.2S wt% to about 10 wt% of dopant, i.e., aluminum. For example, the cathode comprises from about O.S wt% to about S wt% of dopant, i.e., aluminum. In other examples, the cathode comprises from about 1 wt% to about 8 wt% of dopant, i.e., aluminum.
[00085] In another embodiment, the cathode comprises a doped silver powder that has a mean particle diameter of about 20 μm or less. In some embodiments, the cathode comprises a doped silver powder that has a mean particle diameter of about 15 μm or less. For example, the doped silver powder has a mean particle diameter of about 5 μm or less. [00086] In another embodiment, the dopant is present in a sufficient concentration such that cathode has a resistivity of about 30 Ohnvcm or less.
[00087] Cathodes of the present invention comprise silver oxide. For example, the cathode comprises silver powder comprising Ag, AgO, Ag2θ, Ag2Os, AgOH, AgOOH, AgONa, AgCuθ2, AgFeO2, AgMnO2, Ag(OH)2, hydrates thereof, or any combination thereof. In one example, the silver powder comprises Ag2Oa. In another example, the silver powder comprises AgO.
[00088] Cathodes of the present invention can optionally comprise additives such as binders, or other additives to improve one or more features of the cathode. In one example, the cathode comprises a binder. Suitable binders include any binder that is substantially inert to the silver oxide powder or doped silver oxide powder. For example, the binder comprises PTFE or PVDF.
[00089] In another embodiment, a cathode for use in an electrochemical cell comprising a doped silver powder comprising a dopant, wherein the dopant comprises aluminum, and the dopant is present in a sufficient concentration such that cathode has a resistivity of about 30 Ohm*cm or less; and the doped silver oxide powder has a mean particle diameter of about S μm or less.
[00090] Ih another embodiment, a cathode comprises a silver powder that is doped with a sufficient amount of aluminum to provide a resistivity of about 30 Ohnvcm or less and has a mean particle diameter of about 5 μm or less, wherein the silver powder comprises AgO, Ag2θ3, or any combination thereof.
[00091] As noted above, cathodes of the present invention can optionally comprise additives such as binders, current collectors, or the like. In several examples, the cathode of the present invention comprises a binder. For instance, the cathode comprises a binder, and the binder comprises PTFE, PVDF (e.g., PVDF-co-HFP), CMC, PVP, PAA, or a copolymer thereof. [00092] Furthermore cathodes of the present invention comprise silver oxide powder. Silver powder includes Ag, AgO, Ag2O, Ag2Os, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, hydrates thereof, or any combination thereof. [©0093] HL METHODS
[00094] Another aspect of the present invention provides a method of producing a cathode for use in an electrochemical cell comprising providing a silver powder that is doped with from about 0.25 wt% to about 10 wt% of a trivalent dopant by weight of the cathode to give a doped silver powder; and forming the doped silver powder into a cathode.
[00095] Another aspect of the present invention provides a method of producing a cathode for use in an electrochemical cell comprising providing a silver powder that is doped with from about 0.25 wi% to about 10 wt% of a dopant comprising at least one Group 13 element by weight of the cathode to give a doped silver powder; and forming the doped silver powder into a cathode,
[00096] Another aspect of the present invention provides a method of producing a cathode for use in an electrochemical cell comprising providing a silver powder that is doped with from about 0.25 wt% to about 10 wt% of a dopant comprising gallium, boron, indium, aluminum, or any combination thereof by weight of the cathode to give a doped silver powder; and forming the doped silver powder into a cathode.
[Θ0097] Another aspect of the present invention provides a method of producing a cathode for use in an electrochemical cei! comprising providing a silver powder that is doped with from about 0.25 wt% to about 10 wt% of a dopant comprising gallium, boron, or a combination thereof to give a doped silver powder; and forming the doped silver powder into
S] Another aspect of the present invention provides a method of producing a cathode for use in an electrochemical cell comprising providing a silver powder that is doped with from about 0.25 wt% to about 10 wt% of a dopant comprising indium, aluminum, or a combination thereof to give a doped silver powder; and forming the doped silver powder into a cathode.
[00099] In several embodiments of the methods above, the doped silver powder comprises from about 0.5 wt% to about 5 wt% of dopant. In several embodiments of the methods above, the doped silver powder comprises from about 1 wt% to about 8 wt% of dopant. In others, the doped silver powder has a mean particle diameter of about 20 μm or less. And, in some embodiments, the doped silver powder has a mean particle diameter of about 15 μrn or less. For instance, the doped silver powder has a mean particle diameter of about 5 μm or less. In some embodiments of the methods above, the silver powder comprises Ag, AgO, Ag2O, Ag2O3, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, or any combination thereof. In others, the silver powder comprises AgO, Ag2O, Agj€>3, or any combination thereof. In other embodiments of the methods above, the dopant comprises gallium, boron, indium, aluminum, thallium, or any combination thereof. For example, the dopant comprises gallium, boron, or a combination thereof. In other examples, the dopant comprises indium, aluminum, or a combination thereof.
[000100] Some embodiments of the methods above further comprise the step of providing a binder. For example, the method further includes providing a binder and the binder comprises PTFE or PVDF.
[000101] Another aspect of the present invention provides methods of manufacturing a cathode comprising providing a silver powder; and doping the silver powder (e.g., Ag, AgO,
Ag2O, Ag2Oa, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, hydrates thereof, or any combination thereof) with a sufficient amount of dopant such that cathode has a resistivity of about SO Ohm*cm or less, wherein the dopant comprises indium, aluminum, or a combination thereof.
[000102] In several embodiments, the silver powder is doped with a sufficient amount of dopant such that the cathode has a resisitivity of about 40 Ohm*cm or less. For example, the silver powder is doped with a sufficient amount of dopant such that the cathode has a resisitivity of about 35 Ohm«cm or less. Or, the silver powder is doped with a sufficient amount of dopant such that the cathode has a resisitivity of about 30 Ohm»cm or less.
[000103] In some methods, the silver powder is doped with from about 0.25 wt% to about
10 wt% of dopant For example, the silver powder is doped with from about 1 wt% to about
8 wt% of dopant.
[000104] hi other methods, the doped silver powder has a mean particle diameter of about
15 μm or less. For example, the doped silver powder has a mean particle diameter of about 5 μm or less.
[000105] In some alternative methods, the silver powder comprises AgO. Or, the silver oxide powder comprises Ag2Os.
[000106] Methods of the present invention can optionally include providing cathode additives. One exemplary method includes further comprising providing a binder. Suitable binders include any of those mentioned herein. For example, the binder comprises PTFE or
PVDF.
[000107] Another aspect of the present invention provides methods of manufacturing a cathode comprising providing a silver powder; and doping the silver powder with a sufficient amount of dopant such that cathode has a resistivity of about 30 Ohm*cm or less, wherein the dopant comprises aluminum. In some methods, the silver powder is doped with from about 0.25 wt% to about 10 wt% of dopant. For example, the silver powder is doped with from about 1 wt% to about 8 wt% of dopant,
[000109] In oilier methods, the doped silver powder has a mean particle diameter of about 15 μm or less. For example, the doped silver powder has a mean particle diameter of about 5 μm or less.
[§00110] In some alternative methods, the silver powder comprises AgO. Or, the silver oxide powder comprises Ag2θ3.
[IMM)IIl] Methods of the present invention can optionally include providing cathode additives, One exemplary method includes further comprising providing a binder. Suitable binders include any of those mentioned herein. For example, the binder comprises PTFE or
[000112] IV. ELECTROCHEMICAL CELLS
[Θ0Θ113] One aspect of the present invention provides an electrochemical cell comprising a cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein, the dopant comprises a trivalent dopant, and the dopant is present in a sufficient concentration to impart the cell with an actual capacity of at least about 80% (e.g., at least about 85%, or at least about 90%) of the cell's rated capacity over at least 100 cycles (e.g., at least 200 cycles, at least 250 cycles, at least 300 cycles, or at least 400 cycles). [000114] Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein the dopant comprises a trivalent dopant, and the dopant is present in a sufficient concentration to impart the cell with an actual capacity of at least about 60% of the cell's rated capacity over at least about 80 cycles.
[Θ0O115] Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein the dopant comprises at least one Group 13 element, and the dopant is present in a sufficient concentration to impart the cell with an actual capacity of at least about 80% (e.g., at least about 85%, or at least about 90%) of the cell's rated capacity over at least 100 cycles (e.g., at least 200 cycles, at least 250 cycles, at least 300 cycles, at least 350 cycles, or at least 400 cycles).
[000116] Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein the dopant comprises gallium, boron, indium, aluminum, thallium, or any combination thereof, and the dopant is present in a sufficient concentration to impart the cell with an actual capacity of at least about 80% (e.g., at least about 85%, or at least about 90%) of the cell's rated capacity over at least 100 cycles (e.g., at least 200 cycles, at least 250 cycles, at least 300 cycles, at least 350 cycles, or at least 400 cycles). [000117] Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising a silver materia! comprising a dopant; and an anode comprising zinc, wherein the dopant comprises gallium, boron, or a combination thereof, and the dopant is present in a sufficient concentration to impart the cell with an actual capacity of at least about 80% (e.g., at least about 85%, or at least about 90%) of the cell's rated capacity over at least 100 cycles (e.g., at least 200 cycles, at least 250 cycles, at least 300 cycles, at least 350 cycles, or at least 400 cycles),
[000118] Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein the dopant comprises aluminum, indium, or a combination thereof, and the dopant is present in a sufficient concentration to impart the cell with an actual capacity of at least about 80% (e.g., at least about 85%, or at least about 90%) of the cell's rated capacity over at least 100 cycles (e.g., at least, 200 cycles, at least 250 cycles, at least 300 cycles, at least 350 cycles, or at, least 400 cycles).
[000119] In some embodiments, the silver material comprises from about 0.25 wl% to about 10 wt % of trivalent dopant (e.g., at least one Group 13 element (e.g., thallium, boron, gallium, indium, aluminum, or any combination thereof)). In some embodiments, the silver material comprises from about 0.5 wt% to about 5 wt % of trivalent dopant (e.g., at least one Group 13 element (e.g., thallium, boron, gallium, indium, aluminum, or any combination thereof)). In others, the silver material comprises a powder, For instance, the silver material comprises a powder and the powder has a mean particle diameter of about 20 μm or less (e.g., 15 μm or less, 10 μm or less). In other instances, the powder has a mean particle diameter of about 5 μm or less. In other embodiments, the silver powder comprises Ag, AgO, AgyQ, Ag2O3, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, or any combination thereof. In several embodiments, the silver powder comprises AgO, Ag2O, Ag2O3, or any combination thereof. For instance, the silver material comprises AgO. In another instance, the silver material comprises Ag2θ. In other embodiments, the silver material comprises a dopant wherein the dopant comprises gallium, boron, indium, aluminum, or any combination thereof. For example, the silver material comprises a dopant wherein the dopant comprises gallium, boron, or a combination thereof. In another example, the silver material comprises a dopant wherein the dopant comprises indium, aluminum, or a combination thereof. [000120] In other embodiments, the cathode, the anode, or both comprise a binder. For example, in some cells, the cathode comprises a binder. For instance, the cathode comprises a binder and the binder comprises PTFE or PVDF. Ih other examples, the anode comprises a binder. For instance, the anode comprises a binder, and the binder comprises PTFE or PVDF.
[000121] Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising silver powder comprising from about 0.2S wt% to about 10 wt% of a trivalent dopant; an anode comprising zinc; and an electrolyte comprising KOH. [000122] Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising silver powder comprising from about 0.2S wt% to about 10 wt% of at least one Group 13 element by weight of the cathode; an anode comprising zinc; and an electrolyte comprising KOH.
[000123] Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising silver powder comprising from about 0.25 wt% to about 10 wt% of a dopant; an anode comprising zinc; and an electrolyte comprising KOH, wherein the dopant comprises gallium, boron, indium, aluminum, thallium, or any combination thereof. [000124] Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising silver powder comprising from about 0.2S wt% to about 10 wt% of a dopant; an anode comprising zinc; and an electrolyte comprising KOH, wherein the dopant comprises gallium, boron, or a combination thereof. [000125] Another aspect of the present invention provides an electrochemical cell comprising a cathode comprising silver powder comprising from about 0.25 wt% to about 10 wt% of a dopant; an anode comprising zinc; and an electrolyte comprising KOH1 wherein the dopant comprises indium, aluminum, or a combination thereof. [000126] In some embodiments of these aspects, the silver material comprises a powder. For example, silver material comprises a powder, and the powder has a mean particle diameter of about 15 μm or less. In other instances, the powder has a mean particle diameter of about 5 μm or less. In some cathodes of these aspects, the silver powder comprises Ag, AgO, Ag2O, Ag2O3, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, or any combination thereof. For instance, the silver powder comprises AgO, Ag2O, Ag2Os, or any combination thereof . In other instances, the silver material comprises AgO. And, in some instances, the silver material comprises Ag2O. [000127] Ih other embodiments of these aspects, the cathode, the anode, or both comprise a binder. For instance, the cathode comprises a binder. In other instances, cathode comprises a binder, and the binder comprises PTFE or PVDF. In some instances, the anode comprises a binder. For instance, the anode comprises a binder, and the binder comprises PTFE or
PVDF.
[000128] Ih other embodiments of these aspects, the cell further comprises an electrolyte comprising NaOH, KOH, or a combination thereof.
[000129] One aspect of the present invention provides an electrochemical cell comprising a cathode comprising silver powder and a first binder; and an anode comprising zinc and a second binder, wherein the doped silver powder comprises a sufficient amount of indium, aluminum, or a combination thereof to impart the cathode with a resistivity of about SO
Ohm«cm orless.
[000130] One aspect of the present invention provides an electrochemical cell comprising a cathode comprising doped silver powder and a first binder; and an anode comprising zinc and a second binder, wherein the doped silver powder comprises a sufficient amount of indium to impart die cathode with a resistivity of about 30 Ohm«cm or less.
[000131] It is noted that any of the cathodes described herein are suitable for use in electrochemical cells of the present invention.
[000132] In one embodiment, the electrochemical comprises an electrolyte comprising
NaOH or KOH.
[000133] hi another embodiment, the electrochemical cell comprises a cathode comprising doped silver oxide powder comprising from about 0.25 wt% to about 10 wt% of a dopant comprising aluminum and a first binder; an anode comprising zinc and a second binder, and an electrolyte comprising KOH, wherein the cathode has a resistivity of about 30 Ohm • cm or less.
[000134] One aspect of the present invention provides an electrochemical cell comprising a cathode comprising doped silver powder and a first binder; and an anode comprising zinc and a second binder, wherein the doped silver powder comprises a sufficient amount of aluminum to impart the cathode with a resistivity of about 30 Ohm»cm or less.
[000135] It is noted that any of the cathodes described herein are suitable for use in electrochemical cells of the present invention.
[000136] hi one embodiment, the electrochemical comprises an electrolyte comprising
NaOH or KOH. [0(10137] In another embodiment, the electrochemical cell comprises a cathode comprising doped silver powder comprising from about 0.25 wt% to about 10 wt% of a dopant comprising aluminum and a first binder; an anode comprising zinc and a second binder; and an electrolyte comprising KOH, wherein the cathode has a resistivity of about 30 ϋhm*αn or less.
A. Ejggtrodgs
Cathodes and anodes of electrochemical ceils of the present invention can optionally include additives such as a binder, a current collector, or the like. The binder of the cathode and the binder of the anode can include the same material or different materials, In one example, the binder of the anode or the cathode comprises PTFE, PVDF, or any copolymer thereof.
[000140] IΏ cathodes comprising a binder, the binder is admixed with die doped silver powder in a suitable concentration (e.g., less than 10 wt% of binder by weight of the cathode, (e.g., 5 wt% or less of binder by weight of the cathode)) and formed into dough-like material that is shaped to provide the cathode with a suitable size and geometry. It is noted that anodes may likewise be produced using a binder.
[000142] Electrochemical cells of the present invention additionally comprise a separator that is separates the anode from the cathode.
[000143] Separators of the present invention can comprise a film having a single layer or a plurality of layers, wherein the plurality of layers may comprise a single polymer (or copolymer) or more than one polymer (or copolymer).
[000144] In several embodiments, the separators comprise a unitary structure fomiεd from at least two strata. The separator can include strata wherein each layer comprises the same material, or each layer comprises a different layer, or the strata are layered to provide layers of the same material and at least on layer of another material. In several embodiments, one stratum comprises an oxidation resistant material, and the remaining stratum comprises a dendrite resistant material. In other embodiments, at least one stratum comprises an oxidation-resistant material, or at least one stratum comprises a dendrite-resi&tant material. The unitary structure is foπned when the material comprising one stratum (e.g., an oxidation- resistant material) is coextruded with the material comprising another stratum (e.g., a dendrite resistant material or oxidation-resistant material). In several embodiments, the unitary separator is formed from the coextrasion of oxidation-resistant material with dendritε- resistant material. [000145] In several embodiments, the oxidation-resistant materia! comprises a polyetbεr polymer mixture and the dendrite resistant material comprises a PVA polymer mixture, [000146] It is noted that separators useful in electrochemical cells can be configured in any suitable way such thai the separator is substantially inert in the presence of the anode, cathode and electrolyte of the electrochemical cell, For example, a separator for a rectangular battery electrode may be in the form of a sheet or film comparable in size or slightly larger than the electrode, and may simply be placed on the electrode or may be sealed around the edges. The edges of the separator may be sealed to the electrode, an electrode current collector, a battery case, or another separator sheet or film on the backside of the electrode via an adhesive sealant, a gasket, or fusion (heat sealing) of the. separator or another material. The separator may also be in the form of a sheet or film wrapped and folded around the electrode to form a single layer (front and back), an overlapping layer, or multiple layers. For a cylindrical battery, the separator may be spirally wound with the electrodes in a jelly-roll configuration. Typically, the separator is included in an electrode stack comprising a plurality of separators. The oxidation-resistant separator of the invention may be incorporated in a battery in any suitable configuration.
[000147] 1. Polyether Polymer Material
[000148] In several embodiments of the present invention the oxidation-resistant stratum of the separator comprises a polyether polymer material that is coextruded with a dendrite- resistant material. The polyether material can comprise polyethylene oxide (PEO) or polypropylene oxide (PPO), or a copolymer or a mixture thereof. The polyether material may also be copolymerized or mixed with one or more other polymer materials, polyethylene, polypropylene and/or polytetrafluoroethylene (PTFE), for example. In some embodiments, the PE material is capable of forming a free-standing polyether film when extruded alone, or can form a free standing film when coextruded with a dendrite-resistani material. Furthermore, the polyether material is substantially inert in the alkaline battery electrolyte and in the presence of silver ions.
[01)0149] In alternative embodiments, the oxidation resistant material comprises a PE mixture that optionally includes zirconium oxide powder. Without intending to be limited by theory, it is theorized that the zirconium oxide powder inhibits silver ion transport by forming a surface complex with silver ions. The term "zirconium oxide" encompasses any oxide of zirconium, including zirconium dioxide and yttria-stabilized zirconium oxide. The zirconium oxide powder is dispersed throughout the PE material so as to provide a substantially uniform silver complexation and a uniform barrier to transport of silver ions. In several embodiments, the average particle size of the zirconium oxide powder is in the range from about J nm to about 5000 nm, e.g., from about 5 nm to about 100 nm.
[IWOlSO]In other embodiments, the oxidation-resistant materia! further comprises an optional conductivity enhancer. The conductivity enhancer can comprise an inorganic compound, potassium titanate, for example, or an organic material. Titanates of other alkali metals than potassium may be used. Suitable organic conductivity enhancing materials include organic sulfonates and carboxylates. Such organic compounds of sulfonic and carboxylic acids, which may be used singly or in combination, comprise a wide range of polymer materials that may include salts formed wiih a wide variety of electropositive cations, K+, Na+, Li+, Pb+?, Ag÷, NH4+, Ba*\ Sr4/', Mg+2, Ca+/" or anilinium, for example. These compounds also include commercial perfluorinated sulfonic acid polymer materials, Nafion® and Flemion®, for example. The conductivity enhancer may include a sulfonate or carboxylate copolymer, with polyvinyl alcohol, for example, or a polymer having a 2-acrylamido-2-methyl propanyl as a functional group. A combination of one or more conductivity enhancing materials can be used.
[000151]Oxidation-resistant material that is coextruded to form a separator of the present invention can comprise from about 5 wt % to about 95 wt % (e.g., from about 20 wt % to about 60 wt %, or from about 30 wt % to about 50 wt %) of zirconium oxide and/or conductivity enhancer.
[000Ϊ52] Oxidation-resistant materials can also comprise additives such as surfactants that improve dispersion of the zirconium oxide powder by preventing agglomeration of small particles. Any suitable surfactant may be used, including one or more anionic, cationic, non- ionic, ampholytic, amphoteric and zwitterionic surfactants, and mixtures thereof. In one embodiment, the separator comprises an anionic surfactant. For example, the separator comprises an anionic surfactant, and the anionic surfactant comprises a salt of sulfate, a salt of sulfonate, a salt of carboxylate, or a salt of sareosinate. One useful surfactant comprises p- (l,l,3,3-tetramethylbutyl)-phenyl ether, which is commercially available under the trade name Triton X- 100 from Rohm and Haas.
[000153] In several embodiments, the oxidation-resistant material comprises from about 0.01 wt % to about 1 wt % of surfactant. [000154] 2. Polyvinyl Polymer Material
[000155] In several embodiments of the present invention the dendrite-resistant stratum of the separator comprises a polyvinyl polymer material that is coextruded with the oxidation- resistant material. In several embodiments, the PVA material comprises a cross-linked polyvinyl alcohol polymer and a cross-linking agent.
[0(10156] In several embodiments, the cross-linked polyvinyl alcohol polymer is a copolymer, For example, the cross-linked PVA polymer is a copolymer comprising a first monomer, PVA, and a second monomer. In some instances, the PVA polymer is a copolymer comprising at least 60 mole percent of PVA and a second monomer. In other examples, the second monomer comprises vinyl acetate, ethylene, vinyl butyral, or any combination thereof.
[000157] PVA material useful in separators of the present invention also comprise a cross- linking agent in a sufficient quantity as to render the separator substantially insoluble in water. In several embodiments, the cross-Sinking agent used in the separators of the present invention comprises a monoaldehyde (e.g., formaldehyde or glyoxilic acid); aliphatic, furyl or aryl dialdehydes (e.g., glutaraidchyde, 2,6 furyldialdehyde or terephthaldehyde); dicarboxylic acids (e.g., oxalic acid or succinic acid); polyisocyanates; methylolmelamine; copolymers of styrene and maleic anhydride; germaic acid and its salts; boron compounds (e.g., boron oxide, boric acid or its salts; or metaboric acid or its salts); or salts of copper, zinc, aluminum or titanium. For example, the cross-linking agent comprises boric acid. [009158] In another embodiment, the PVA material optionally comprises zirconium oxide powder. In several embodiments, the PVA material comprises from about 1 wt % to about 99 wt % (e.g., from about 2 wt % to about 98 wt %, from about 20 wt % to about 60 wt %, or from about 30 wt % to about 50 wt %).
[000159] in many embodiments, the dendrite-resistant strata of the separator of the present invention comprises a reduced ionic conductivity. For example, in several embodiments, the separator comprises an ionic resistance of less than about 20 rnΩ/cm^, (e.g., less than about 10 mΩ/cm2, less than about 5 mΩ/cra2, or less than about 4mΩ/cm2). [000160] The PVA material that forms the dendrite-resistant stratum of the separator of the present invention can optionally comprise any suitable additives such as a conductivity enhancer, a surfactant, a plasticizer, or the like.
[ΘΘΘ161J In some embodiments, the PVA material further comprises a conductivity enhancer. For example, the PVA material comprises a cross-linked polyvinyl alcohol polymer, a zirconium oxide powder, and a conductivity enhancer. The conductivity enhancer comprises a copolymer of polyvinyl alcohol and a hydroxyl-conducting polymer. Suitable hydroxyl-conducting polymers have functional groups that facilitate migration of hydroxyl ions. In some examples, the hydroxyl- conducting polymer comprises polyacrylate, polylactone, polysulfonate, polycarboxylate, polysulfate, polysarconate, polyaraide. polyamidosulfonate, or any combination thereof. A solution containing a copolymer of a polyvinyl alcohol and a poiylactone is sold commercially under the trade name Vytek polymer by Celanese, Inc. In several examples, the separator comprises from about 1 wt % to about 10 wi % of conductivity enhancer,
[000162] In other embodiments, the PVA material further comprises a surfactant. For example, the separator comprises a cross-linked polyvinyl alcohol polymer, a zirconium oxide powder, and a surfactant. The surfactant comprises one or more surfactants selected from an anionic surfactant, a catioiiic surfactant, a nonionic surfactant, an ampholytic surfactant, an amphoteric surfactant, and a zwitterionic surfactant. Such surfactants are commercially available, ϊn several examples, the PVA material comprises from about 0.01 wt % to about 1 wt % of surfactant.
[000163] In several embodiments, the dendrite-resistant stratum further comprises a plasticizer. For example, the dendrite-resistant stratum comprises a cross-linked polyvinyl alcohol polymer, a zirconium oxide powder, and a plasticizer. The plasticizer comprises one or more plasticizers selected from glycerin, low-molecular-weight polyethylene glycols, aminoalcohols, polypropylene glycols, 1,3 pentanediol branched analogs, 1,3 pentanediol, and/or water. For example, the plasticizer comprises greater than about 1 wt % of glycerin, low- molecular- weight polyethylene glycols, aminoalcohols, polypropylene glycols, 1,3 pentanediol branched analogs, 1,3 pentanediol. or any combination thereof, and less than 99 wt % of water. In other examples, the plasticizer comprises from about 1 wt % to about 10 wt % of glycerin, low-molecular-weight polyethylene glycols, aminoalcohols, polypropylene glycols, 1,3 pentanediol branched analogs, 1,3 pentanediol, or any combination thereof, and from about 99 wt % to about 90 wt % of water.
[000164] ϊn some embodiments, the separator of the present invention further comprises a plasticizer. In other examples, the plasiicizer comprises glycerin, a low-molecular-weight polyethylene glycol, an aminoalcohol, a polypropylene glycols, a 1.3 pentanediol branched analog, 1.3 pentanediol, or combinations thereof, and/or water. [0§0165] C. Ejectrolylgs
[OiMH 66] Electrochemical cells of the present invention can comprise any suitable electrolyte. For example, the electrochemical cell comprises an electrolyte that includes aqueous NaOH or KOH. In other examples, the electrolyte comprises a mixture of NaOH or KOH and a liquid PEO polymer.
[000167] Electrolytes that are suited to electrochemical cells of the present invention include an alkaline agent. Exemplary electrolytes include aqueous metal-hydroxides such as NaOH and/or KOH. Other exemplary electrolytes include mixtures of a metal hydroxide and a polymer that has a glass transition temperature below the range of operating and/or storage temperatures for the electrochemical cell into which it employed (e.g. at least -20 0C). [000168] Polymers useful far formulating an electrolyte of the present invention are also at least substantially miscible with an alkaline agent. In one embodiment, the polymer is at least substantially miscible with the alkaline agent over a range of temperatures that at least includes the operating and storage temperatures of the electrochemical device in which the mixture is used. For example, the polymer is at least substantially miscible, e.g., substantially miscible with the alkaline agent at a temperature of at least -20 0C. In other examples, the electrolyte has a glass transition temperature of at least -IS 0C (e.g., at least -12 0C, at least - 10 0C, or from about -20 0C to about 700C). In another embodiment, the polymer is at least substantially miscible with the alkaline agent at a temperature from about -20 0C to about 60 0C. For example, the polymer is at least substantially miscible with the alkaline agent at a temperature of from about -100C to about 6O0C.
[000169] Ih several embodiments, the polymer can combine with the alkaline agent at a temperature in the range of temperatures of the operation of the electrochemical device in which is it stored to form a solution.
[000170] hi one embodiment, the electrolyte comprises a polymer of formula (I):
Figure imgf000030_0001
wherein each of Ri, R2, R3, and R4 is independently (Vi-Qi-V2-Q2-V3-Q3)B1 each of Vi, V2, and V3, is independently a bond or -O-, each of Qi, Q2, and Qj, is independently a bond, hydrogen, or a CMJ linear or branched unsubstituted alkyl, n is 1-5, and p is a positive integer of sufficient value such that the polymer of formula (I) has a total molecular weight of less than 10,000 amu (e.g., less than about SOOO amu, less than about 3000 amu, from about SO amu to about 2000 amu, or from about 100 amu to about 1000 amu) and an alkaline agent. [000171] Ih several embodiments, the polymer is straight or branched. For example, the polymer is straight hi other embodiments, Ri is independently (Vi-Qi-V2-Qz-Vs-Qj)n, wherein n is 1, each of Vi, Qi, V2, Q2, and V3 is a bond, and Qj is hydrogen. In some embodiments, R4 is independently (Vi-Qi-Va-Qj-V3-Qj)n, wherein n is 1, each of V], Qi, V2, Q2, and V3, is a bond, and Q3 is hydrogen. In other embodiments, both of Ri and R4 are (Vi- Qi-V2-Q2-V3-Qj)n, each n is 1, each of Vj, Qi, V2, Q2, and V3 is a bond, and each Q3 is hydrogen. [000172] However, in other embodiments, Rt is independently (Vi-Qi-V2-Q2-V3-Qs)n, wherein n is 1, each of Vi, Qi, V2, Q2, and V3 is abond, and Q3 is -CH3, -CH2CH3, -
CH2CH2CH3, or H. For example, Ri is independently (Vi-Q1-V2-Ch-V3-Qs)Ii, wherein n is I1 each of Vi, Qi, V2, Q2, and V3 is a bond, and Q3 is -CH3 or H.
[000173] In another example, Ri is independently (VrQi-V2-Q2-VB-Qs)n. wherein n is 1, one of Qi or Q2 is -CH2-, -CH2CH2-, or -CH2CH2CH2-; Vi and V2 are each a bond; V3 is -O-, and
Q3 is H.
[000174] In several other examples R4 is independently (Vi-Qi-V2-Ch-Vs-Qs)n, wherein n is
1, each of Vi, Qi, V2, Q2, is a bond, and V3 is -O- or a bond, and Q3 is hydrogen, -CH3, -
CH2CH3, or -CH2CH2CH3. For example, R4 is independently (Vi-Qi-V2-Q2-V3-Q3)B, wherein n is I1 each of Vi, Qi, V2, Q2, and V3 is a bond, and Q3 is -H, -CH3, -CH2CH3, or -
CH2CH2CH3.
[000175] In another embodiment, Ri is (Vi-QrV2-Q2-V3-Qs)n, wherein n is 1, each of Vi,
Qi, V2, Q2, and V3 is a bond, and Q3 is -CH3, and R4 is (VrQi-V2-Q2-V3-Q3),,, wherein n is 1, each of Vi, Qi, V2, Q2, is a bond, and V3 is -O-, and Q3 is -H.
[000176] In some embodiments, R2 is independently (VrQi-V2-Q2-V3-Q3)Q, wherein n is 1, each of Vi, Qi, V2, Q2, and V3 is a bond, and Q3 is -CH3, -CH2CH3, -CH2CH2CH3, or H. In other embodiments, R2 is independently (V]-QrV2-Ch-V3-Q3),,, wherein n is 1, one of Vi, Qi,
V2, Q2, and V3 is -O-, and Q3 is -H.
[000177] In some embodiments, R3 is independently (VrQi-V2-Q2-V3-Q3),,, wherein n is I1 each of Vi, Qi, V2, Q2, and V3 is a bond, and Q3 is -CH3, -CH2CH3, -CH2CH2CH3, or H. In other embodiments, R3 is independently (VrQi-Va-Ch-V3-Qj)n, wherein n is 1, one of Vi, Q],
V2, Q2, and V3 is -O-, and Q3 is -H.
[000178] Li some embodiments, the polymer comprises a polyethylene oxide. In other examples, the polymer comprises a polyethylene oxide selected from polyethylene glycol, polypropylene glycol, polybutylene glycol, alkyl-polyethylene glycol, alkyl-polypropylene glycol, alkyl-polybutylene glycol, and any combination thereof.
[000179] In another embodiment, the polymer is a polyethylene oxide having a molecular weight or mean molecular weight of less than about 10,000 amu (e.g., less than about 5000 amu, or from about 100 amu to about 1000 amu). In other embodiments, the polymer comprises polyethylene glycol.
[000180] Alkaline agents useful in the electrolyte of the present invention are capable of producing hydroxyl ions when mixed with an aqueous or polar solvent such as water and/or a liquid polymer. [000181] In some embodiments, the alkaline agent comprises LiOH, NaOH, KOH, CsOH, RbOH, or combinations thereof. For example, the alkaline agent comprises LiOH, NaOH, KOH, or combinations thereof. In another example, the alkaline agent comprises KOH. [000182] Ih several exemplary embodiments, the electrolyte of the present invention comprises a liquid polymer of formula (I) and an alkaline agent comprising LiOH, NaOH, KOH, CsOH, RbOH, or combinations thereof. In other exemplary embodiments, the electrolyte comprises a liquid polymer comprising a polyethylene oxide; and an alkaline agent comprising LiOH, NaOH, KOH, CsOH, RbOH, or combinations thereof. For example, the electrolyte comprises a polymer comprising a polyethylene oxide and an alkaline agent comprising KOH.
[000183] In several exemplary embodiments, the electrolyte of the present invention comprises more than about 1 wt % of alkaline agent (e.g., more than about 5 wt % of alkaline agent, or from about S wt % to about 76 wt % of alkaline agent). Ih one example, the electrolyte comprises a liquid polymer comprising a polyethylene oxide and 3 wt % or more (e.g., 4 wt % or more, from about 4 wt % to about 33 wt %, or from about 5 wt % to about IS wt %) of an alkaline agent For instance, the electrolyte comprises polyethylene oxide and 5 , wt % or more of KOH. In another example, the electrolyte consists essentially of a polyethylene oxide having a molecular weight or mean molecular weight from about 100 amu to about 1000 amu and S wt % or more of KOH.
[000184] Electrolytes useful in the present invention can be substantially free of water. Ih several embodiments, the electrolyte comprises water in an amount of about 60 % of the wt of the alkaline agent or less (e.g., about SO % of the wt of the alkaline agent or less, about 40 % of the wt of the alkaline agent or less, about 30 % of the wt of the alkaline agent or less, about 25 % of the wt of the alkaline agent or less, about 20 % of the wt of the alkaline agent or less, or about 10 % of the wt of the alkaline agent or less).
[000185] Exemplary alkaline polymer electrolytes include, without limitation, 90 wt % PEG- 200 and 10 wt % KOH, SO wt % PEG-200 and 50 wt % KOH; PEG-dimethyl ether that is saturated with KOH; PEG-dimethyl ether and 33 wt % KOH; PEG-dimethyl ether and 11 wt % KOH; and PEG-dimethyl ether (mean molecular weight of 500 amu) and 33 wt % KOH, that is further diluted to 11 wt % KOH with PEG-dimethyl ether having a mean molecular weight of 200 amu.
[000186] Optionally, electrolytes of the present invention can also comprise less than about 10 wt% by weight of electrolyte (e.g., less than about 5 wt% by weight of electrolyte or less than about 1 wt% by weight of electrolyte) of a small carbon chain alcohol such as methanol, ethanol, isopropanol, or mixtures thereof.
[000187] In some examples, the electrolyte is aqueous KOH, For instance 8M KOH, 12M
KOH, or the like.
[000188] In other examples, the electrolyte is aqueous NaOH. For instance 8M NaOH, 12M
NaOH, or the like.
D. Cell Housing
Cells of the present invention can include any suitable housing such that the housing does not substantially impede electrical access to the terminals of the cell, In some embodiments, the cell housing comprises flexible packaging material Usually, the flexible packaging material is used in a sachet configuration or a drawn cavity configuration. Unlike traditional applications of flexible packaging battery packaging requires feed through to carry the current from the enclosed electrochemical cell. Insulating and sealing these feed- throughs can be done by a number of methods, Typical, the flexible packaging material consists of three functional layers, which can be embodied in three physical layer or less (e.g., in some packaging materials, the physical layers perform one, two, or three of the functions performed by functional layers). The first functional layer is an electrolyte compatible layer, This layer provides chemical resistance and physical containment of the liquid or gelatinous electrolyte. Typically this layer can consist of a polyolefm or polyethyl vinyl alcohol that may be co-extruded or mixed with an adhesion promoter, ethyl acrylic acid for example, to facilitate heat sealing or current feed-through adhesion. The second functional layer is a vapor barrier layer. This layer can be a metal, aluminum, or a low transmissibility polymer. This functional layer needs to retard the diffusion of water, electrolyte solvent, oxygen, hydrogen, and carbon dioxide into the cell. The third functional layer, provide a physical integrity layer on the outside of the packaging. It provides much of the packaging materials strength and abrasion resistance. This layer may also provide the physical strength to allow the packaging material to be formed into blisters. This layer is typically nylon or mylar in its composition. The functional layer materials can also be applied as conformal coatings to the cells by dip coating or spraying. Cells packaged in flexible packaging typically contain a reduced pressure atmosphere with the absolute pressure inside less than ambient pressure. [00019I] V. EXAMPLES:
[0ΘΘ192] The following materials were used to produce exemplary cathodes, test cathodes, and/or exemplary electrochemical cells of the present invention:
[000193] Example No. 1: Undoped AgO Cathode For Use as Experimental Control A
[000194] The following material and methods were used to generate undoped AgO cathode material that was used in cells for purposes of generating comparative data concerning cell performance characteristics, i.e., cell cycle life. The undoped AgO cathode material generated using the methods of example no. 1 serves as a control for comparison purposes.
[000195] Materials:
Silver nitrate: A.C.S. grade, DFG
Gelatin: from bovine skin, type B, ~225 bloom, Sigma
Potassium hydroxide solution: KOH solution, 1.4g/ml, LabChem., Inc.
Potassium persulfate, 99+%, Sigma-Aldrich
Procedures: Example: undoped AgO
[000196] A 2L Aceglass reactor was placed into a hot water bath and a Teflon-coated radial propeller was used. 116.7 g of AgNθ3 and 1000 g of DI water were added to the reactor and stirred at 400 rpm. The mixture in the reactor was heated to 55 0C. 0.11 g gelatin was added. In a plastic container, 240 g of KOH solution (1.4g/ml) was mixed with 240 g Dl water to give a diluted KOH solution. The diluted KOH solution was added to the reactor per pump at 550C. At 65 0C, 198 g of potassium persulfate was added and the temperature was maintained for 50 min.
[000197] The water was decanted as the solution cooled down and the particles settled. The particles were rinsed with DI water, and once the particles settled, the water was decanted. The particles underwent this rinse and decant process until the ion conductivity of the mixture measured below 25 micro-Ohm. The product was filtered and dried in a 60 0C vacuum oven. [000198] The resultant undoped AgO cathode material is characterized below in Table 1.
Table 1: Undoped AgO cathodes.
[000199] The activity of cathode materials described in Table 1 was measured by titration: [000200] A sample was crushed with a spatula. If sample was not completely dry, it was dried in a vacuum oven at 60 0C overnight. 0.100 g of sample was added to a clean 12S ml flask, wherein the weight was measured accurately to at least the third decimal place. 10 ml of acetate buffer and 5 ml KI solution was added to the flask. The flask was swirled to disperse particles followed by covering the flask by putting an inverted plastic cup over top, and sonicating for 2 hours. 20 ml of DI was added to the flask. The solution was titrated with Na2S2U3 until the solution achieved a pale yellow (record exact normality). Approximately 1 ml of starch indicator was added and titration continued until the solution achieved a milky whitish-yellow endpoint [000201] The following equation was used to calculate activity:
Figure imgf000035_0001
[000202] Particle size analysis was performed using a Horiba LA-930. Diameters on 10%, 50%, and 95% (DlO, D50, and D95) were measured for the samples provided above and below.
[000203] The resistivities of this cathode material was measured using the following procedure: 3 grams of sample material was loaded into a powder compression cell with a 3,88 cm2 electrode surface area. Force was applied to the sample from 10 to 40 tons by using a laboratory hydraulic press. The resistance was recorded every 5 tons and the thickness of the sample at 40 tons is also recorded. The resistivity of the sample is the resistance value extrapolated to infinite force divided by final material thickness and multiplied by the area of the powder cell electrodes.
[000204] Example No. 2: Exemplary In-Doped Cathodes of the Present Invention [000205] A 4000 ml Erlenmeyer flask was placed into a hot water bath and a Teflon-coated radial propeller was used for stirring. 301.5 g of AgNC^ and 2500 g of DI water were added to the reaction flask and stirred at 300 rpm. 2.85 g Indium (ID) Nitrate Pentahydrate was dissolved in 100 g DI water and added to the flask. The mixture in the flask was heated to 50 0C.
[000206] In a plastic container, 800 g of KOH solution (1.4g/ml) was mixed with 50 g DI water to give a diluted KOH solution. The diluted KOH solution was added to the reaction flask all at once. The mixture was heated to 65 0C, and 544.8 g of potassium persulfate was added. Then, the flask was heated to 75 0C for 15 min. When the solution cooled down and the particles settled, the water was decanted. The particles were rinsed with DI water, and once the particles settled, the water was decanted. The particles underwent this rinse and decant process until the ion conductivity of the mixture dropped below 25 micro-Ohm. [000207] This process generated 219.6 g of 1.3 wt% In doped AgO (assuming 100% yield). [000208] The following exemplary cathodes, described in Table 2, were generated by adjusting the amount of Indium (HI) Nitrate Pentahydrate used in the procedure described above.
Table 2: Exemplary cathodes of the present invention comprising indium dopant.
Figure imgf000036_0001
[000209] Activities, resistivities, and particle sizes were measured as described in Example No. 1.
[000210] Example No. 3: Pb-coated AgO Cathode For Use as Experimental Control B [000211] Under stirring, 2.6 wt% lead acetate trihydrate solution was slowly added to a 20 wt% suspension of AgO in de-ionized water. The resulting suspension was allowed to settle, and the water was decanted. The residue was re re-suspend with de-ionized water and decanted. This decanting process was repeated several times and then filtered. The filtrate was dried in vacuum oven at 600C. This process was used to generate standard process yields of about 100 g of Pb-coated AgO, which was used as a test cathode material for evaluating properties of the cathode materials described in Example 1, above. [000212] Example No.4: Evaluation of Exemplary Cathode Materials of Example No.2 [000213] A cathodes prepared in Example No. 2 was employed in an electrochemical cell, depicted in FIGURE 1, to evaluate the effect of the dopant on a cell's cycle life. The cell's cycle life was ascertained by repeatedly cycling the cell attendant to a charge - discharge algorithm wherein the freshly prepared cell, having a 100% SOC equal to about 100% of its rated capacity, is discharged to about 100% of its depth of discharge, i.e., discharged to about 100% DOD, and then re-charged to about 100% SOC, wherein it is again discharged to about 100% DOD. During each cycle, the actual capacity of the cell, i.e., the cell's capacity at 100% SOC, was observed and used to develop a plot of the cell's actual capacity against the number of charge cycles in which the cell was subjected. Figure 2 presents a partial plot of one such evaluation. Using plots of this type, the number of charge cycles at which the cell's actual capacity was observed to be about 70%, about 80%, about 90%, or the like, of the cell's rated capacity can be observed. In conducting these evaluations, tests cells were constructed as described below.
[000214] Test cells were constructed, as depicted in FIGURE 1, using cathodes incorporating the exemplary cathode material described in Example No, 2 and comparative cells, e.g., control cells, were constructed including a cathode that included the cathode material described in Example No. 3 in one comparative cell and cathode material described in Example No. 1 in a second comparative cell. Each of the cells were constructed from the following materials:
[000216] Anode Active Material was formulated from 81.9 % Zinc, 5 % PTFE binder
[DuPont TE3859], 12.7 % zinc oxide (AZO66), 0.45% Bi2O3, to give a final mass of 3.6 g,
Each of these ingredients was obtained from commercial sources.
[000217] Anode Current Coilector: in/brass 32 (80/20), 43 mm x 31 mm, pressed at 2T, a commercial product of Dexmet.
[00021S] Anode Adsorber Wrap: Solupor (commercially available from Lydall, Inc. of
Rochester N.H.)
[000220] Cathode Active material was formulated from 3% PTFE binder (DuPont TE3859) and cathode material from Example Nos. 1, 2, or 3, depending on the cell, to give a filial mass of 5.85 g.
[000221] Cathode Current Collector: silver, commercial product of Dexmεt. Cathode was pressed at 5.5T.
[000222] Cathode Adsorber Wrap: SL6-8 (commercially available from Shanghai Shllong
Hi-Tech Co., LTD.)
[000223] Electrode Separators: 2 adjacent separators were employed wherein one separator was formed from Innovia 32(80/20) soaked with 1 ml electrolyte and the second separator was formed from Innovia 32(80/20) (separator materials are commercially available from
Innoviafϊlms, Ltd. of Wigton, Cumbria, U.K.).
[000224] Electrolyte: 32% by weight aqueous KOH and NaOH mixture (80/20 mol ratio)
[0002251 Cell housing
[000225] Aluminum laminated Him (D-EWOH(II)) from Pred Material International was used as cell housing.
[000227] Each of the cells was evaluated via charge-discharge cycle testing, wherein the cells were charged to about 100% of their rated capacities and discharged of the cells' actual capacity. The results of this testing is provided in Table 3 below:
Table 3: Results of charge-discharge cycle testing for In-doped AgO cathodes.
Figure imgf000038_0001
[000228] The results of the test cell employing the Pb-coated AgO cathode is provided in Table 4:
Table 4: Results of charge-discharge cycle testing for Pb-coated AgO cathode.
Figure imgf000038_0002
[000229] FIGURE 2 presents the charge profiles for the test cells including the Pb-Coated AgO test cathode material and 2.0 wt% In doped AgO cathode material for comparison. [000230] Example No. 5: Exemplary AI-Doped Cathodes of the Present Invention [000231] A 4000 ml Erlenmeyer flask was placed into a hot water bath and a Teflon-coated radial propeller was used for stirring. 301.5 g of AgNOa and 2500 g of DI water were added to the reaction flask and stirred at 300 rpm. 2.85 g aluminum hydroxide was dissolved in 100 g DI water and added to the flask. The mixture in the flask was heated to 50 0C. [000232] Li a plastic container, 800 g of KOH solution (1.4g/ml) was mixed with 50 g DI water to give a diluted KOH solution. The diluted KOH solution was added to the reaction flask all at once. The mixture was heated to 65 0C, and 544.8 g of potassium persulfate was added. Then, the flask was heated to 75 0C for 15 min. When the solution cooled down and the particles settled, the water was decanted. The particles were rinsed with DI water, and once the particles settled, the water was decanted. The particles underwent this rinse and decant process until the ion conductivity of the mixture dropped below 25 micro-Ohm. [000233] This process generated 219.6 g of 1.3 wt% Al doped AgO (assuming 100% yield). [000234] Example No.6: Exemplary 0.9% Ga-Doped Cathodes of the Present Invention [000235] The following methods were used to generate AgO doped with 0.9 % gallium. [000236] Materials:
Silver nitrate: A.C.S. grade, DFG
Gallium (III) nitrate hydrate: 99.9% metals basis, Aldrich
Gelatin from bovine skin, type B, -225 bloom, Sigma
Potassium hydroxide solution: KOH solution, 1.4g/ml, LabChem., Inc.
Potassium persulfate, 99+%, Sigma-Aldrich
[000237] A 2L Aceglass reactor was placed into a hot water bath and a Teflon-coated radial propeller was used. 116.7 g of AgNO3 and 1000 g of DI water were added to the reactor and stirred at 400 rpm. 0.77 g Gallium (EU) nitrate hydrate was dissolved in 100 g DI water and added to the reactor. The mixture in the reactor was heated to 55 0C. 0.11 g gelatin was added. In a plastic container, 240 g of KOH solution (1.4 g/ml) was mixed with 240 g DI water to give a diluted KOH solution. The diluted KOH solution was added to the reactor per pump at 55 0C. The mixture was heated to 65 0C, 198 g of potassium persulfate was added, and the temperature was maintained for 50 min. The water was decanted as the solution cooled down, and the particles settled. The particles were rinsed with DI water, and once the particles settled, the water was decanted. The particles underwent this rinse and decant process until the ion conductivity of the mixture measured below 25 micro-Ohm. The product was filtered and dried in a vacuum oven at 60 0C.
[000238] The following exemplary cathode, described in Table 5, was generated using the procedure described above: Table 5: Exemplary cathode material of the present invention comprising gallium dopant.
Figure imgf000040_0001
[000239] Activities, resistivities, and particle sizes were measured according to the procedures described in Example No. 1.
[000240] Example No.7: Evaluation of Exemplary Cathode Materials of Example No.6 [000241] Test cells and comparative cells were constructed and evaluated as described above in Example No.4 and FIGURE 1, wherein the test cell was formulated as described above, substituting the cathode material of Example No. 6 for the cathode material of Example No. 2 in the test cell, and employing a comparative cell described above using a cathode material of Example No. 1. The life cycle data comparison of test cell incorporating Ga-doped cathode material of Example No.6 and the comparative cathode incorporating the cathode material of Example No. 1 is presented in Table 6:
Table 6: Results of charge-discharge cycle testing for Ga-doped AgO cathode and undoped
AgO cathode.
Figure imgf000040_0002
[000242] Example No. 8: Exemplary 1.3% B-Doped Cathodes of the Present Invention
[000243] Materials:
Silver nitrate: A.C.S. grade, DFG
Boron oxide: 99.98%, Sigma-Aldrich
Gelatin: from bovine skin, type 6, -225 bloom, Sigma
Potassium hydroxide solution: KOH solution, 1.4g/ml, LabChem., Inc.
Potassium persulfate, 99+%, Sigma-Aldrich
[000244] A 2L Aceglass reactor was placed into a hot water bath and a Teflon-coated radial propeller was used. 116.7 g of AgNO3 and 1000 g of DI water were added to the reactor and stirred at 400 rpm. 1.11 g Boron oxide was dissolved in 100 g DI water and added to the reactor. The mixture in the reactor was heated to 55 0C. 0.11 g gelatin was added. Ih a plastic container, 240 g of KOH solution (1.4g/ral) was mixed with 240 g DI water to give a diluted KOH solution. The diluted KOH solution was added to the reactor per pump at 550C. At 65 0C, 198 g of potassium persulfate was added, and add the temperature was maintained for 50 min.
[000245] The water as decanted as the solution cooled down, and the particles settled. The panicles were rinsed with DI water, and once the particles settled, the water was decanted. The particles underwent this rinse and decant process until the ion conductivity of the mixture dropped below 25 micro-Ohm. The product was filtered and dried in a 600C vacuum oven. [000246] The following physical properties of Boron-doped AgO were tested, and results were summarized in the Table 7:
Table 7: Exemplary cathode of the present invention comprising boron dopant.
Figure imgf000041_0001
Silver nitrate: A.C.S. grade, DFG
Ytterbium (III) nitrate pentahydrate, 99.9% metal basis, Aldrich
Gelatin: from bovine skin, type B, -225 bloom, Sigma
Potassium hydroxide solution: KOH solution, 1.4g/ml, LabChem., Inc.
Potassium persulfate, 99-1-%, Sigma- Aldrich
A 2L Aceglass reactor was placed into a hot water bath and a Teflon-coated radial propeller was used. 116,7 g of AgNO3 and 1000 g of DI water were added to the reactor and stirred at 400 rpm. 3.06 g Ytterbium (111) nitrate pentahydrate was dissolved in 100 g Dl water and added to the reactor. The mixture in the reactor was heated to 55 0C. 0.11 g gelatin was added.
[000250] In a plastic container, 240 g of KOH solution (1.4g/ml) was mixed with 240 g DI water to give a diluted KOH solution. The dilated KOH solution was added to the reactor per pump at 55 0C. The mixture was heated to 65 0C and 198 g of potassium persulfate was added. This temperature was maintained for 50 min.
[000251] The water was decanted as the solution cooled and the particles settled. The particles were rinsed with DI water, and once the particles settled, the water was decanted. The particles underwent this rinse and decant process until the ion conductivity of the mixture dropped below 25 micro-Ohm. The product was filtered and dried in a 60 0C vacuum oven. [000252] The resistivity of the above cathode material was measured to be 38 Ω.cm, as measured using the method described above in Example No. I, above. [000253] Example No. 10: Evaluation of Exemplary Cathode Materials of Example No. 8
[000254] Test cells were constructed and evaluated as described above in Example Nos.4 and 7 wherein the test cells were formulated as described above, substituting the cathode material of Example No. 8 in the test cell or Example No. 1 in the comparative cell. The life cycle data comparison of test cell incorporating B-doped cathode material of Example No. 8 and the comparative cathode incorporating the cathode material of Example No. 1 is presented in Table 8:
Table 8: Results of charge-discharge cycle testing for B-doped AgO cathode and undoped
AgO cathode.
Figure imgf000042_0001
OTHER EMBODIMENTS
[000255] All publications and patents referred to in this disclosure are incorporated herein by reference to the same extent as if each individual publication or patent application were specifically and individually indicated to be incorporated by reference. Should the meaning of the terms in any of the patents or publications incorporated by reference conflict with the meaning of the terms used in this disclosure, the meaning of the terms in this disclosure are intended to be controlling. Furthermore, the foregoing discussion discloses and describes merely exemplary embodiments of the present invention. One skilled in the art will readily recognize from such discussion and from the accompanying drawings and claims, that various changes, modifications and variations can be made therein without departing from the spirit and scope of the invention as defined in the following claims.

Claims

What is claimed is:
1. A cathode for use in an electrochemical cell comprising a silver material that is doped with a trivalent dopant to give a doped silver material, wherein the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the doped silver material.
2. The cathode of claim 1, further comprising from about 0.5 wt% to about 5 wt% of trivalent dopant.
3. The cathode of either of claims 1 or 2, wherein the doped silver material comprises a powder.
4. The cathode of claim 3, wherein the powder has a mean particle diameter of about 20 μm or less.
5. The cathode of either of claims 3 or 4, wherein the powder has a mean particle diameter of about 5 μm or less.
6. The cathode of any of claims 1-5, wherein the silver material comprises Ag, AgO, Ag2O, Ag2O3, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, or any combination thereof.
7. The cathode of any of claim 1-6, further comprising a binder.
8. The cathode of claim 7, wherein the binder comprises FTFE or FVDF.
9. The cathode of any of claims 1-8, wherein the dopant comprises at least one Group 13 element.
10. The cathode of any of claims 1-9, wherein the dopant comprises aluminum, indium, gallium, boron, thallium, or any combination thereof.
11.. The cathode of any of claims 1-8, wherein the dopant comprises a lanthanide element
12. The cathode of claim 11, wherein the lanthanide element is Yb.
13. A cathode for use in an electrochemical cell comprising a doped silver material comprising a dopant, wherein the dopant comprises gallium, boron, or a combination thereof, and the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of die doped silver material.
14. The cathode of claim 13, further comprising from about 0.5 wt% to about 5 wt% of dopant.
15. The cathode of either of claims 13 or 14, wherein the doped silver material comprises a powder.
16. The cathode of claim IS, wherein the powder has a mean particle diameter of about 20 μm or less.
17. The cathode of either of claims IS or 16, wherein the powder has a mean particle diameter of about 5 μm or less.
18. The cathode of any of claims 13-17, wherein the silver material comprises Ag, AgO, Ag2O, Ag2O3, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, or any combination thereof.
19. The cathode of any of claim 13-18, further comprising a binder.
20. The cathode of claim 19, wherein the binder comprises PTFE or PVDF.
21. The cathode of any of claims 13-20, wherein the dopant comprises gallium.
22. The cathode of any of claims 13-20, wherein the dopant comprises boron.
23. A cathode for use in an electrochemical cell comprising a doped silver material comprising a dopant, wherein the dopant comprises indium, aluminum, or a combination thereof, and the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the doped silver material.
24. The cathode of claim 23, further comprising from about 1 wt% to about 8 wt% of
25. The cathode of either of claims 23 or 24, wherein the doped silver material comprises a powder.
26. The cathode of claim 25, wherein the powder has a mean particle diameter of about 20 μm or less.
27. The cathode of either of claims 25 or 26, wherein the powder has a mean particle diameter of about 5 μm or less.
28. The cathode of any of claims 23-27, wherein the doped silver material comprises Ag1 AgO, Ag2O, AgA, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, or any combination thereof.
29. The cathode of any of claim 23-28, further comprising a binder.
30. The cathode of claim 29, wherein lhe binder comprises PTFE or PVDF.
31. The cathode of any of claims 23-30, wherein the dopant comprises indium.
32. The cathode of any of claims 23-30, wherein the dopant comprises aluminum.
33. A method of producing a cathode for use in an electrochemical cell comprising providing a silver powder that is doped with from about 0.25 wt% to about 10 wt% of a trivalent dopant by weight of the silver powder to give a doped silver powder, and forming the doped silver powder into a cathode.
34. The method of claim 33, wherein the doped silver powder is doped with from about 0.5 wt% to about S wt% of dopant.
35. The method of either of claims 33 or 34, wherein the doped silver powder has a mean particle diameter of about 15 μm or less.
36. The method of any of claims 33-3S, wherein the doped silver powder has a mean particle diameter of about S μm or less.
37. The method of any of claims 33-36, wherein the doped silver powder comprises Ag, AgO, Ag2O, Ag2O3, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, or any combination thereof.
38. The method of any of claims 33-37, wherein the doped silver powder comprises AgO, Ag2O, Ag2θ3, or any combination thereof.
39. The method of any of claim 33-38, further comprising providing a binder.
40. The method of claim 40, wherein the binder comprises PTFE or PVDF.
41. The method of any of claims 33-41, wherein the dopant comprises a lanthanide element.
42. The method of claim 42, wherein the lanthanide element is Yb.
43. The method of any of claims 33-41 , wherein the dopant comprises at least one Group 13 element
44. The method of any of claims 33-41 or 44, wherein the dopant comprises gallium, boron, indium, aluminum, thallium, or any combination thereof. -
45. The method of any of claims 33-41, 44, or 45, wherein the dopant comprises gallium, boron, or a combination thereof.
46. The method of any of claims 33-41 or 44-46, wherein the dopant comprises indium, aluminum, or a combination thereof.
47. An electrochemical cell comprising a cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein the dopant comprises a trivalent dopant, and the dopant is present in a sufficient concentration to impart tbe cell with an actual capacity of at least about 60% of the cell's rated capacity over at least about 80 cycles.
48. An electrochemical cell comprising a cathode comprising a silver material comprising a dopant; and an anode comprising zinc, wherein the dopant comprises a trivalent dopant, and the dopant is present in a sufficient concentration to impart the ceil with an actual capacity of at least about 70% of the cell's rated capacity over at least about 100 cycles.
49. An electrochemical cell comprising a cathode comprising a silver material comprising a dopant; and an anodε comprising zinc, wherein the dopant comprises a trivaient dopant, and the dopant is present in a sufficient concentration to impart the cell with an actual capacity of at least about 80% of the cell's rated capacity over at least about 120 cycles.
50. The cell of any of claims 47-49, wherein the silver material comprises from about 0.25 wt% to about 10 wt % of trivalent dopant by weight of silver material
51. The cell of any of claims 47-50, wherein the silver material comprises a powder.
52. The cell of claim 51, wherein the powder has a mean particle diameter of about 20 μm or less.
53. The cell of claim 52, wherein the powder has a mean particle diameter of about 5 μm or less.
54. The cell of any of claims 47-53, wherein the cathode, the anode, or both comprise a binder.
55. The cell of any of claims 47-54, wherein the cathode further comprises a binder.
56. The cell of claim 55, wherein the binder comprises PTFE or PVDF.
57. The cell of any of claims 47-54, wherein the anode further comprises a binder.
58. The cell of claim 57, wherein the binder comprises PTFE or PVDF.
59. The cell of any of claims 47-58, further comprising an electrolyte comprising NaOH, KOH, or a combination thereof.
60. The cell of any of claims 47-59, wherein the silver powder comprises Ag, AgO1 Ag2O, Ag2O3, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, or any combination thereof.
61. The cell of any of claims 47-60, wherein the silver powder comprises AgO, Ag2O, Ag2O3, or any combination thereof.
62. The cell of any of claims 47-61, wherein the silver material comprises AgO.
63. The cell of any of claims 47-61, wherein the silver material comprises Ag2O.
64. The cell of any of claims 47-63, wherein the dopant comprises a lanthanide element.
65. The cell of claim 64, wherein the lathanide element is Yb.
66. The cell of any of claims 47-63, wherein the dopant comprises at least one Group 13 element.
67. The cell of claim 66, wherein the dopant comprises indium, aluminum, gallium, boron, thallium, or any combination thereof.
68. The cell of claim 67, wherein the dopant comprises indium, aluminum, or a combination thereof.
69. The cell of claim 67, wherein the dopant comprises gallium, boron, or a combination thereof.
70. An electrochemical cell comprising: a cathode comprising a silver powder comprising from about 0.25 wt% to about 10 wt% of a trivalent dopant by weight of the silver powder; an anode comprising zinc; and an electrolyte comprising aqueous KOH.
71. The cell claim 70, wherein the silver powder has a mean particle diameter of about 20 μm or less.
72. The cell of claim 71, wherein the silver powder has a mean particle diameter of about 5 μm or less.
73. The cell of any of claims 70-72, wherein the cathode, the anode, or both comprise a binder.
74. The cell of any of claims 70-73, wherein the cathode comprises a binder.
75. The cell of claim 74, wherein the binder comprises FTFE or PVDF.
76. The cell of any of claims 70-73, wherein the anode comprises a binder.
77. The cell of claim 76, wherein the binder comprises PTFE or PVDF.
78. The cell of any of claims 70-77, further comprising an electrolyte comprising NaOH, KOH, or a combination thereof.
79. The cell of any of claims 70-78, wherein the silver powder comprises Ag, AgO, Ag2O, Ag2O3, AgOH, AgOOH, AgONa, AgCuO2, AgFeO2, AgMnO2, Ag(OH)2, or any combination thereof.
80. The cell of any of claims 70-79, wherein the silver powder comprises AgO, Ag2O, Ag2θ3, or any combination thereof.
81. The cell of any of claims 70-80, wherein the silver material comprises AgO.
82. The cell of any of claims 70-80, wherein the silver material comprises Ag2O.
83. The cell of any of claims 70-82, wherein the dopant comprises at least one Group 13 element.
84. The cell of any of claims 70-83, wherein the dopant comprises indium, aluminum, gallium, boron, thallium, or any combination thereof.
85. The cell of any of claims 70-84, wherein the dopant comprises indium, aluminum, or a combination thereof.
86. The cell of any of claims 70-84, wherein the dopant comprises gallium, boron, or a combination thereof.
87. A cathode for use in an electrochemical cell comprising a doped silver material comprising a dopant, wherein the dopant comprises a lanthanide element, aluminum, indium, gallium, boron, or a combination thereof, and the dopant is present in a concentration of from about 0.2S wt% to about 10 wt% by weight of the doped silver material.
88. The cathode of claim 87, wherein the lanthanide element is Yb.
89. A cathode for use in an electrochemical cell comprising a doped silver material comprising a dopant, wherein the dopant comprises a lanthamde element, and the dopant is present in a concentration of from about 0.25 wt% to about 10 wt% by weight of the doped silver material.
90. The cathode of claim 89, wherein the lanthanide element comprises Yb.
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9184444B2 (en) 2009-11-03 2015-11-10 Zpower, Llc Electrodes and rechargeable batteries
US9401509B2 (en) 2010-09-24 2016-07-26 Zpower, Llc Cathode
US9799886B2 (en) 2012-09-27 2017-10-24 Zpower, Llc Cathode with silver material and silicate dopant and method of producing
DE102020205393A1 (en) 2020-04-29 2021-11-04 Siemens Aktiengesellschaft Bimetallic and multimetallic catalysts for the selective electroreduction of CO2 and / or CO to hydrocarbons and oxygenates

Families Citing this family (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8936775B2 (en) 2008-10-29 2015-01-20 Zpower, Llc Cathode active material (higher oxides of silver)
WO2012061449A1 (en) 2010-11-03 2012-05-10 Zpower, Llc Novel electrodes and rechargeable batteries
US10559827B2 (en) 2013-12-03 2020-02-11 Ionic Materials, Inc. Electrochemical cell having solid ionically conducting polymer material
WO2016197098A1 (en) 2015-06-04 2016-12-08 Ionic Materials, Inc. Solid state bipolar battery
US11319411B2 (en) 2012-04-11 2022-05-03 Ionic Materials, Inc. Solid ionically conducting polymer material
US11251455B2 (en) 2012-04-11 2022-02-15 Ionic Materials, Inc. Solid ionically conducting polymer material
US9819053B1 (en) 2012-04-11 2017-11-14 Ionic Materials, Inc. Solid electrolyte high energy battery
US11152657B2 (en) 2012-04-11 2021-10-19 Ionic Materials, Inc. Alkaline metal-air battery cathode
EP3813157A1 (en) 2013-12-03 2021-04-28 Ionic Materials, Inc. Solid, ionically conducting polymer material, and applications
KR102385977B1 (en) 2014-04-01 2022-04-13 아이오닉 머터리얼스, 인코퍼레이션 High capacity polymer cathode and high energy density rechargeable cell comprising the cathode
EP3304636A4 (en) 2015-06-04 2018-11-07 Ionic Materials, Inc. Lithium metal battery with solid polymer electrolyte
KR102607433B1 (en) 2015-06-08 2023-11-27 아이오닉 머터리얼스, 인코퍼레이션 Battery with aluminum anode and solid polymer
US11342559B2 (en) 2015-06-08 2022-05-24 Ionic Materials, Inc. Battery with polyvalent metal anode
KR20210059795A (en) * 2016-05-27 2021-05-25 아이오닉 머터리얼스, 인코퍼레이션 Electrochemical cell having solid ionically conducting polymer material
EP3574542A4 (en) 2017-01-26 2020-09-02 Ionic Materials, Inc. Alkaline battery cathode with solid polymer electrolyte
US10448137B1 (en) 2018-06-21 2019-10-15 Bose Corporation Dual zone discharge of rechargeable batteries

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5611860A (en) * 1979-07-07 1981-02-05 Hitachi Maxell Ltd Silver-oxide secondary-battery
US5585208A (en) * 1995-08-10 1996-12-17 Lian; Keryn K. Alkaline gel electrolyte for electrochemical cells
US6287432B1 (en) * 1987-03-13 2001-09-11 The Standard Oil Company Solid multi-component membranes, electrochemical reactor components, electrochemical reactors and use of membranes, reactor components, and reactor for oxidation reactions
US20040101729A1 (en) * 2001-04-19 2004-05-27 Kearl Daniel A. Hybrid thin film/thick film solid oxide fuel cell and method of manufacturing the same
US20080038630A1 (en) * 2005-03-25 2008-02-14 Michael Cheiky Rechargeable AgO cathode

Family Cites Families (106)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2528891A (en) 1945-03-26 1950-11-07 Herbert E Lawson Primary battery depolarizer and method of making the same
US3057944A (en) 1959-12-21 1962-10-09 Electric Storage Battery Co Electric battery
USRE25608E (en) 1959-12-21 1964-06-30 cahan
US3062909A (en) * 1960-06-06 1962-11-06 Electric Storage Battery Co Fuel cell electrode
GB1065059A (en) * 1962-12-17 1967-04-12 Electric Storage Battery Co Improvements relating to storage battery electrodes
US3325311A (en) * 1964-05-19 1967-06-13 Allis Chalmers Mfg Co Preparation of a boron-doped silver oxygen electrode
US3954501A (en) 1974-01-10 1976-05-04 Guy Rampel Rechargeable electrodes utilizing unsintered fluorocarbon binder
US3920478A (en) * 1974-06-25 1975-11-18 Union Carbide Corp Divalent silver oxide-zinc cell having a unipotential discharge level
US4015056A (en) 1976-03-15 1977-03-29 Esb Incorporated Method of manufacturing a stable divalent silver oxide depolarizer mix
IL50024A (en) 1976-07-12 1979-05-31 Israel State Secondary cells
JPS5380530A (en) * 1976-12-24 1978-07-17 Suwa Seikosha Kk Flat battery
FR2376526A1 (en) 1976-12-30 1978-07-28 Accumulateurs Fixes POSITIVE ACTIVE MATERIAL FOR ELECTRIC BATTERIES
US4056664A (en) 1977-01-28 1977-11-01 P. R. Mallory & Co. Inc. Electrochemical cell having an AgO electrode discharging at an Ag2 O voltage level
US4078127A (en) 1977-04-21 1978-03-07 Esb Incorporated Additive for an alkaline battery employing divalent silver oxide positive active material
CH630492A5 (en) 1977-04-28 1982-06-15 Leclanche Sa ALKALINE PRIMARY CELL.
JPS547537A (en) 1977-06-20 1979-01-20 Hitachi Maxell Silver oxide primary cell
JPS5937546B2 (en) * 1977-06-22 1984-09-10 松下電器産業株式会社 alkaline battery
DE2757583C2 (en) 1977-12-23 1984-10-25 Varta Batterie Ag, 3000 Hannover Galvanic cell with alkaline electrolyte and process for its manufacture
DE2813149A1 (en) 1978-03-25 1979-09-27 Varta Batterie Continuous mfr. of active silver oxide for batteries - by treatment of silver nitrate or argentous oxide with ozone
US4167609A (en) 1978-03-30 1979-09-11 Union Carbide Corporation Zinc oxide additive for divalent silver oxide electrodes
CA1127707A (en) * 1978-03-30 1982-07-13 Union Carbide Corporation Aluminum additive for cells using divalent silver oxide electrodes
CH639512A5 (en) 1978-07-06 1983-11-15 Leclanche Sa LOW-WATER ALKALINE PRIMARY CELL WITH LONG LIFE.
US4298506A (en) 1978-11-03 1981-11-03 Duracell International Inc. Method of treating silver oxide powder and the product formed therefrom
JPS5596556A (en) * 1979-01-19 1980-07-22 Mitsubishi Electric Corp Silver oxide battery
EP0021735B1 (en) 1979-06-26 1984-12-05 LUCAS INDUSTRIES public limited company Zinc electrode for secondary electrochemical cells and electrochemical cells including said electrode
US4288733A (en) 1979-10-17 1981-09-08 Black & Decker Inc. Battery charger system and method adapted for use in a sterilized environment
JPS56149771A (en) * 1980-04-19 1981-11-19 Hitachi Maxell Ltd Silver-oxide secondary battery
JPS5765671A (en) * 1980-10-09 1982-04-21 Sumitomo Metal Mining Co Ltd Silver peroxide battery
US4338385A (en) * 1980-06-23 1982-07-06 Sumitomo Metal Mining Company, Ltd. Divalent silver oxide cell containing cadmium and tellurium components
JPS57107565A (en) * 1980-12-25 1982-07-05 Sumitomo Metal Mining Co Ltd Silver peroxide battery
US4327157A (en) 1981-02-20 1982-04-27 The United States Of America As Represented By The Secretary Of The Navy Stabilized nickel-zinc battery
JPS58119156A (en) * 1982-01-11 1983-07-15 Seiko Instr & Electronics Ltd Silver peroxide battery
JPS58152373A (en) * 1982-03-05 1983-09-09 Seiko Instr & Electronics Ltd Silver peroxide cell
JPS59132567A (en) * 1983-01-20 1984-07-30 Seiko Instr & Electronics Ltd Silver peroxide battery
JPS59184459A (en) * 1983-04-01 1984-10-19 Sumitomo Metal Mining Co Ltd Silver peroxide battery
US4465747A (en) 1983-06-29 1984-08-14 Union Carbide Corporation Alkali metal or alkaline earth metal compound additive for manganese dioxide-containing nonaqueous cells
JPS60189164A (en) 1984-03-06 1985-09-26 Matsushita Electric Ind Co Ltd Silver oxide battery
US4835077A (en) 1986-02-05 1989-05-30 Rayovac Corporation AgO cathode material
US5240793A (en) 1988-12-07 1993-08-31 Grillo-Werke Ag Alkaline batteries containing a zinc powder with indium and bismuth
US5017446A (en) 1989-10-24 1991-05-21 Globe-Union Inc. Electrodes containing conductive metal oxides
US5108852A (en) 1990-03-23 1992-04-28 Battery Technologies Inc. Manganese dioxide cathode for a rechargeable alkaline cell, and cell containing the same
US5336384A (en) 1991-11-14 1994-08-09 The Dow Chemical Company Membrane-electrode structure for electrochemical cells
HU914046D0 (en) 1991-12-19 1992-04-28 Environmetal Batteries Systems Cylindrical alkaline manganese dioxide zinc cell with improved lower sealing
HUT67932A (en) 1991-12-19 1995-05-29 Environmental Batteries System Alkaline manganese dioxide cell of low mercury content or withot mercury
DE69303091T2 (en) 1992-03-26 1997-01-23 Japan Vilene Co Ltd Battery separator and battery
US5558680A (en) 1992-11-23 1996-09-24 Wilson Greatbatch Ltd. Preparation of silver vanadium oxide cathodes utilizing sol-gel technology
US5290640A (en) 1993-03-10 1994-03-01 Acme Electric Corporation Sealed rechargeable battery
US5516340A (en) 1993-03-17 1996-05-14 Wilson Greatbatch Ltd. Process for making a metal oxide composite cathode material for high energy density batteries
JP3445654B2 (en) 1993-03-17 2003-09-08 ウィルソン グレイトバッチ リミテッド Electrochemical cell and its cathode
US5389469A (en) 1993-06-14 1995-02-14 Rayovac Corporation AgO battery, and material
US6001508A (en) 1993-06-14 1999-12-14 Rayovac Corporation AgO cathode battery
US5393617A (en) 1993-10-08 1995-02-28 Electro Energy, Inc. Bipolar electrochmeical battery of stacked wafer cells
JPH07302597A (en) 1994-04-29 1995-11-14 Mine Safety Appliances Co Lithium battery
US5525444A (en) 1994-06-27 1996-06-11 Toshiba Battery Co., Ltd. Alkaline secondary battery
US5599644A (en) 1995-06-07 1997-02-04 Eveready Battery Company, Inc. Cathodes for electrochemical cells having additives
US5837402A (en) * 1995-12-21 1998-11-17 Dowa Mining Co., Ltd. Zinc powders for use in batteries and a secondary alkaline zinc battery using said zinc powders
JP3703582B2 (en) 1996-02-22 2005-10-05 呉羽化学工業株式会社 Electrode binder, electrode binder solution, electrode mixture, electrode structure and battery
JPH09320589A (en) * 1996-06-03 1997-12-12 Sony Corp Silver oxide battery
US5981105A (en) 1996-07-08 1999-11-09 Emf Systems, Inc. High rate metal oxide electrodes
CA2267319A1 (en) 1996-10-11 1998-04-23 Massachusetts Institute Of Technology Polymer electrolyte, intercalation compounds and electrodes for batteries
JP2001506400A (en) 1997-01-31 2001-05-15 メルク パテント ゲゼルシャフト ミット ベシュレンクテル ハフトング Novel manganese dioxide electrode, its production method and its use
US7625420B1 (en) * 1997-02-24 2009-12-01 Cabot Corporation Copper powders methods for producing powders and devices fabricated from same
JP4473967B2 (en) 1997-03-04 2010-06-02 日本ゼオン株式会社 Binder for battery, binder composition for battery, slurry for battery electrode, electrode for lithium secondary battery, and lithium secondary battery
EP0898317B1 (en) 1997-08-22 2007-03-21 Wilson Greatbatch Ltd. Cathode comprising a mixed phase metal oxide, method of preparation and electrochemical cell therefor
US6153337A (en) 1997-12-19 2000-11-28 Moltech Corporation Separators for electrochemical cells
IL124007A (en) 1998-04-08 2001-08-26 Univ Ramot Long cycle-life alkali metal battery
JP3173594B2 (en) 1998-08-31 2001-06-04 株式会社ファインセル Zinc sulfate aqueous solution secondary battery to which manganese salt (II) and carbon powder are added
JP2000164220A (en) 1998-11-26 2000-06-16 Mitsubishi Materials Corp Electrode material for silver oxide battery
US6228534B1 (en) 1998-12-21 2001-05-08 Wilson Greatbatch Ltd. Annealing of mixed metal oxide electrodes to reduce polarization resistance
KR100367284B1 (en) 1999-02-22 2003-01-09 티디케이가부시기가이샤 Secondary Battery, and its Production Process
AU4024800A (en) 1999-03-29 2000-10-16 Gillette Company, The Alkaline cell with improved separator
JP2001185116A (en) 1999-12-28 2001-07-06 Oji Paper Co Ltd Separator for battery and alkaline secondary cell
JP2001202958A (en) * 2000-01-17 2001-07-27 Mitsubishi Materials Corp Silver oxide-carbon composite material and active material for positive electrode of silver oxide secondary battery and producing method of silver oxide-carbon composite material
US6589612B1 (en) 2000-05-10 2003-07-08 The Gillette Company Battery and method of making the same
US6794082B2 (en) * 2000-09-08 2004-09-21 Sony Corporation Alkaline battery
AU772305B2 (en) 2000-09-11 2004-04-22 Dowa Mining Co. Ltd. Positive electrode active material for alkaline cell
FR2817076A1 (en) 2000-11-20 2002-05-24 Atofina MICROCOMPOSITE POWDER BASED ON AN ELECTRICAL CONDUCTOR AND A FLUOROPOLYMER AND OBJECTS MADE WITH THIS POWDER
US6797019B2 (en) 2000-12-15 2004-09-28 Wilson Greatbatch Ltd. Electrochemical cell having an electrode of silver vanadium oxide coated to a current collector
US6743548B2 (en) * 2001-04-19 2004-06-01 Zinc Matrix Power, Inc. Silver-zinc alkaline rechargeable battery (stacking order)
US7501208B2 (en) 2001-06-01 2009-03-10 Eveready Battery Company, Inc. Doped manganese dioxides
US20030113630A1 (en) * 2001-12-06 2003-06-19 Kainthla Ramesh C. Anodic zinc electrode for use in an alkaline based electrochemical cell
US7214443B2 (en) 2002-02-12 2007-05-08 Plurion Limited Secondary battery with autolytic dendrites
US6803151B2 (en) 2002-02-21 2004-10-12 Delphi Technologies, Inc. Electrode
US6759166B2 (en) 2002-05-06 2004-07-06 The Gillette Company Alkaline cell with improved cathode
JP4135074B2 (en) 2002-10-25 2008-08-20 ソニー株式会社 Negative electrode manufacturing method and battery manufacturing method
JP4262475B2 (en) 2002-12-27 2009-05-13 三菱化学株式会社 Negative electrode material and negative electrode for non-aqueous lithium ion secondary battery, and non-aqueous lithium ion secondary battery
US7132062B1 (en) 2003-04-15 2006-11-07 Plasticolors, Inc. Electrically conductive additive system and method of making same
US7201888B2 (en) 2003-10-07 2007-04-10 Ferro Corporation Nanosized silver oxide powder
JP4739691B2 (en) 2004-05-13 2011-08-03 パナソニック株式会社 Alkaline battery
US9012096B2 (en) 2004-05-28 2015-04-21 Uchicago Argonne, Llc Long life lithium batteries with stabilized electrodes
US7300722B2 (en) * 2005-04-11 2007-11-27 The Gillette Company Lithium battery containing bismuth metal oxide
KR100668353B1 (en) 2006-02-07 2007-01-12 삼성에스디아이 주식회사 Metal catalyst and a fuel cell employing an electrode including the same
FR2903529B1 (en) 2006-07-05 2008-10-17 Conseil Et De Prospective Scie NEW POSITIVE SILVER ELECTRODE FOR ALKALINE ACCUMULATORS
US7972726B2 (en) 2006-07-10 2011-07-05 The Gillette Company Primary alkaline battery containing bismuth metal oxide
WO2008039419A2 (en) 2006-09-25 2008-04-03 Zpower Inc. Oxidation-resistant separator for zinc-silver oxide batteries
US7976976B2 (en) 2007-02-07 2011-07-12 Rosecreek Technologies Inc. Composite current collector
US20100119941A1 (en) 2007-04-02 2010-05-13 Koninklijke Philips Electronics N.V. Electrochemical energy source and electronic device provided with such an electrochemical energy source
US20080261094A1 (en) 2007-04-20 2008-10-23 Stuart Licht Stabilized electrodes for electrochemical cells
WO2009120352A1 (en) 2008-03-27 2009-10-01 Zpower, Inc. Improved electrodes and electrochemical cells employing the same
WO2009120351A1 (en) 2008-03-27 2009-10-01 Zpower, Inc. Polymer electrolytes
US8936775B2 (en) 2008-10-29 2015-01-20 Zpower, Llc Cathode active material (higher oxides of silver)
CN102484249A (en) 2009-08-27 2012-05-30 安维亚系统公司 Layer-layer lithium rich complex metal oxides with high specific capacity and excellent cycling
CA2779090A1 (en) 2009-11-03 2011-05-12 Zpower, Llc Novel electrodes and rechargeable batteries
US9401509B2 (en) 2010-09-24 2016-07-26 Zpower, Llc Cathode
WO2012061449A1 (en) 2010-11-03 2012-05-10 Zpower, Llc Novel electrodes and rechargeable batteries
DK2901516T3 (en) 2012-09-27 2017-09-11 Zpower Llc cathode

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5611860A (en) * 1979-07-07 1981-02-05 Hitachi Maxell Ltd Silver-oxide secondary-battery
US6287432B1 (en) * 1987-03-13 2001-09-11 The Standard Oil Company Solid multi-component membranes, electrochemical reactor components, electrochemical reactors and use of membranes, reactor components, and reactor for oxidation reactions
US5585208A (en) * 1995-08-10 1996-12-17 Lian; Keryn K. Alkaline gel electrolyte for electrochemical cells
US20040101729A1 (en) * 2001-04-19 2004-05-27 Kearl Daniel A. Hybrid thin film/thick film solid oxide fuel cell and method of manufacturing the same
US20080038630A1 (en) * 2005-03-25 2008-02-14 Michael Cheiky Rechargeable AgO cathode

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP2411563A4 *

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9184444B2 (en) 2009-11-03 2015-11-10 Zpower, Llc Electrodes and rechargeable batteries
US9401509B2 (en) 2010-09-24 2016-07-26 Zpower, Llc Cathode
US9799886B2 (en) 2012-09-27 2017-10-24 Zpower, Llc Cathode with silver material and silicate dopant and method of producing
DE102020205393A1 (en) 2020-04-29 2021-11-04 Siemens Aktiengesellschaft Bimetallic and multimetallic catalysts for the selective electroreduction of CO2 and / or CO to hydrocarbons and oxygenates

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JP2012522336A (en) 2012-09-20
US9209454B2 (en) 2015-12-08
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AU2010229828B2 (en) 2014-07-03
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