[go: up one dir, main page]

US20160204441A1 - Wall Mounted Zinc Batteries - Google Patents

Wall Mounted Zinc Batteries Download PDF

Info

Publication number
US20160204441A1
US20160204441A1 US14/840,020 US201514840020A US2016204441A1 US 20160204441 A1 US20160204441 A1 US 20160204441A1 US 201514840020 A US201514840020 A US 201514840020A US 2016204441 A1 US2016204441 A1 US 2016204441A1
Authority
US
United States
Prior art keywords
zinc
module
battery
nickel
rechargeable
Prior art date
Legal status (The legal status 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 status listed.)
Abandoned
Application number
US14/840,020
Inventor
Iakov Kogan
Anna Khomenko
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
PANISOLAR Inc
Original Assignee
PANISOLAR 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 PANISOLAR Inc filed Critical PANISOLAR Inc
Priority to US14/840,020 priority Critical patent/US20160204441A1/en
Priority to US15/081,885 priority patent/US10608243B2/en
Publication of US20160204441A1 publication Critical patent/US20160204441A1/en
Abandoned legal-status Critical Current

Links

Images

Classifications

    • 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
    • H01M4/244—Zinc electrodes
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/04—Hybrid capacitors
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/22—Electrodes
    • H01G11/30—Electrodes characterised by their material
    • H01G11/46—Metal oxides
    • 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
    • H01M10/26—Selection of materials as electrolytes
    • 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
    • H01M10/30—Nickel accumulators
    • 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
    • H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/4235—Safety or regulating additives or arrangements in electrodes, separators or electrolyte
    • H01M12/005—
    • H01M2/0262—
    • H01M2/14—
    • 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
    • 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
    • H01M4/32—Nickel 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
    • H01M4/24—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
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
    • 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
    • H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/42—Alloys based on zinc
    • 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
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • 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
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/52—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
    • 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
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/54—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of silver
    • 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
    • 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
    • H01M4/64—Carriers or collectors
    • H01M4/66—Selection of materials
    • H01M4/661—Metal or alloys, e.g. alloy coatings
    • 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
    • H01M4/64—Carriers or collectors
    • H01M4/70—Carriers or collectors characterised by shape or form
    • 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
    • H01M4/64—Carriers or collectors
    • H01M4/70—Carriers or collectors characterised by shape or form
    • H01M4/80—Porous plates, e.g. sintered carriers
    • H01M4/808—Foamed, spongy materials
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10—Primary casings; Jackets or wrappings
    • H01M50/116—Primary casings; Jackets or wrappings characterised by the material
    • H01M50/117—Inorganic material
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10—Primary casings; Jackets or wrappings
    • H01M50/116—Primary casings; Jackets or wrappings characterised by the material
    • H01M50/117—Inorganic material
    • H01M50/119—Metals
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10—Primary casings; Jackets or wrappings
    • H01M50/116—Primary casings; Jackets or wrappings characterised by the material
    • H01M50/121—Organic material
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10—Primary casings; Jackets or wrappings
    • H01M50/116—Primary casings; Jackets or wrappings characterised by the material
    • H01M50/124—Primary casings; Jackets or wrappings characterised by the material having a layered structure
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10—Primary casings; Jackets or wrappings
    • H01M50/147—Lids or covers
    • H01M50/155—Lids or covers characterised by the material
    • H01M50/16—Organic material
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409—Separators, membranes or diaphragms characterised by the material
    • H01M50/411—Organic material
    • H01M50/414—Synthetic resins, e.g. thermoplastics or thermosetting resins
    • H01M50/417—Polyolefins
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409—Separators, membranes or diaphragms characterised by the material
    • H01M50/44—Fibrous material
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/18—Regenerative fuel cells, e.g. redox flow batteries or secondary fuel cells
    • H01M8/184—Regeneration by electrochemical means
    • H01M8/188—Regeneration by electrochemical means by recharging of redox couples containing fluids; Redox flow type batteries
    • 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
    • H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/027—Negative 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
    • H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/028—Positive electrodes
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2220/00—Batteries for particular applications
    • H01M2220/10—Batteries in stationary systems, e.g. emergency power source in plant
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2220/00—Batteries for particular applications
    • H01M2220/20—Batteries in motive systems, e.g. vehicle, ship, plane
    • 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
    • H01M4/04—Processes of manufacture in general
    • H01M4/0402—Methods of deposition of the material
    • H01M4/0404—Methods of deposition of the material by coating on electrode collectors
    • 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
    • H01M4/26—Processes of manufacture
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10—Energy storage using batteries
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/50—Fuel cells

Definitions

  • This invention proposes thin ( ⁇ 1 cm) home wall energy storage devices based on zinc-air and nickel-zinc batteries with replaceable and rechargeable zinc modules.
  • Zinc batteries which are low cost, high energy and safe to operate, are prospective storage devices for reserve power, electric grid, and transportation.
  • Nickel oxide-hydroxide cathodes also referred as nickel cathodes
  • Batteries with nickel oxide-hydroxide cathodes are attractive because of long cycle life of the nickel electrode.
  • Linden's Handbook of Batteries specifies lifetime of nickel-cadmium batteries as 8-25 years.
  • the cadmium electrode has been phasing out from mass production because of safety concerns.
  • Nickel-metal hydride batteries that have replaced nickel-cadmium storage devices are more expensive that nickel-cadmium batteries.
  • Nickel-zinc batteries have 30% higher energy density in comparison with nickel-metal hydride devices.
  • a nickel-zinc battery with the cost about $300/KWh and power capabilities of a lithium battery, ten years lifetime, and 5,000-7,500 charge-discharge cycles can be considered as effective substitute for large-sized lithium batteries.
  • Zinc-air batteries are the cheapest (based on cost per energy density) batteries at market, and allows very high specific energies up to 280 Wh/kg.
  • Rechargeable zinc-air batteries have two basic designs: a) batteries with bifunctional air-electrodes, and b) batteries with dual air electrodes. In case of dual air electrodes one electrode is used for air reduction while another one for oxygen evolution. In case of rechargeable batteries with dual air electrodes the growth of metal dendrites is localized between metal and oxygen evolution electrodes. As the result no dendrites appear at the interface between zinc and oxygen reduction electrodes what eliminates short circuits during discharge.
  • the use of dual air electrodes allows better selection and optimization of current collectors as well as catalysts to insure better cycle life of the storage devices.
  • a battery with dual air electrode is described by Tzidon et al in WO Pat. No. 2012/156872 A1.
  • This battery has six electrodes: two zinc, two air (reduction), and two oxygen evolution electrodes.
  • a metal-air battery assembled from elemental cells is arranged face-to-face, and requires leaving air gaps about 1 mm-2 mm to allow air access to the whole surface of the air electrode. Taking into account that the thickness of an elemental cell is about (or less) than 10 mm, the presence of air gaps increases battery volume by 10%-20%.
  • Rechargeable batteries with zinc anodes have cycle life about 500-900 cycles.
  • This invention uses rechargeable and replaceable zinc cartridges as components of nickel-zinc batteries.
  • the cycle life of the batteries can be increased by replacing zinc cartridges at about 10% of the battery cost.
  • As the result the total lifetime of the anode can be extended to be compatible with that of the nickel-oxide hydroxide cathode.
  • the home wall battery design includes rotational joints to assure zinc cartridge replacement without disassembling the batteries.
  • Zinc composition is formulated using additives of polyphenylenediamines and zirconium hollow fibers. A flat module with battery/supercapacitor characteristics has been demonstrated.
  • FIG. 1 shows horizontal cross section of a nickel-zinc cell with replaceable and rechargeable zinc anodes.
  • the cell includes the nickel oxide hydroxide electrode 1 , the cell wall 2 , the zinc anode 3 , the electrolyte 4 , the separator 5 and the base 6 .
  • An individual cell is specified as 7 .
  • FIG. 2 demonstrates a flat module made of the cells 7 .
  • FIG. 3 illustrates a foldable module where the cells 7 are joined with the flexible tubes 8 .
  • FIG. 4 displays a portion of the module base with pockets 9 , grooves 10 ; and connection holes 11 .
  • FIG. 5 demonstrates a portion of the module base printed by a 3d printer; the picture shows grooves 10 , and honeycomb structure 12 .
  • FIG. 6A shows the front view of a wall mounted battery assembled from three modules connected using rotational joints 13 .
  • FIG. 6B shows the side view of the wall mounted battery with rotational joints 13 .
  • FIG. 6C shows the side view of the wall mounted battery where joints 13 are rotated to replace zinc anodes 3 .
  • FIG. 7 shows an example of a circuit that commutates three cells.
  • Each cell includes an oxygen reduction (OR), metal (Me) and oxygen evolution (OE) electrodes, multiple relays with control contacts 14 ; the circuit also includes switch 15 , and optional resistor 16 .
  • OR oxygen reduction
  • Me metal
  • OE oxygen evolution
  • FIG. 8 shows practical implementation of a zinc-air module made of three cells, and controlled by a dual three position relay 17 .
  • FIG. 9 shows cycling profile of a zinc-air module made of three cells
  • Low cost rechargeable zinc cartridges are intended to be used as the components of the nickel-zinc battery. After degradation an old zinc cartridge is replaced by a new one at about 10% of the battery cost to serve the next period. As the result the capital cost of the battery is increased by 10% for the second period, but not by 100% when the battery is replaced completely.
  • FIG. 1 shows horizontal cross section of a nickel-zinc cell with replaceable zinc anode.
  • the cell includes the nickel oxide hydroxide electrode 1 , the cell wall 2 , the zinc anode 3 , the electrolyte 4 , the separator 5 and the base 6 .
  • the cell can include two nickel anodes fixed as the cell walls.
  • a replaceable zinc cartridge is formed of zinc electrode 3 that includes a current collector and zinc electrode composition, and sealed with separator envelop 4 .
  • the thickness of the cartridge is selected in such a way that it fits free space (pocket) of the cell, and can be moved out of the cell without any physical or functional damage to the electrode.
  • Typical thickness of the zinc cartridge is in the interval from 0.1 mm to 1 cm.
  • the cartridges with lower/larger thickness will also work, but might be unpractical.
  • the idea of a replaceable electrode is applicable to any other rechargeable electrode that can be used with nickel-metal and metal-air batteries.
  • a replaceable and rechargeable anode can be formed from iron, cobalt, cadmium, nickel hydride, or the alloys of metals.
  • the idea can be applied to other batteries like silver-zinc battery if a high cycle life silver electrode is available.
  • the replacement of the zinc cartridge can be performed when the battery (and the nickel electrode) is discharged.
  • a new zinc electrode which replaces old one, should be also in the discharged state.
  • This can be achieved by formulation of the zinc electrode on the basis of doped zinc oxide and additives.
  • a zinc electrode formed from zinc powder can be chemically or electrochemically discharged before moving into discharged nickel-zinc battery.
  • the zinc cartridge can also be replaced when the nickel electrode is in the charged state; in this case a charged zinc electrode is used to complement the state of charge of the nickel electrode.
  • Zinc cartridge includes a zinc electrode wrapped in the separator, or in the anion-exchange membrane.
  • the separator/membrane envelope is hermetically sealed, so that ions can exchange with electrolyte solely through the separator or membrane or a combination thereof.
  • Separator is made from a porous material stable in alkaline solutions. Examples of separator materials include polyethylene, polypropylene, and cellophane. Such a porous material can include a thin layer of an anion exchange material.
  • the zinc electrode can be formed from zinc powder, or zinc oxide doped with lead, bismuth, indium, aluminum or other metals that inhibit hydrogen evolution during charging.
  • Zinc or zinc oxide paste can also include carboxymethylcellulose, polyvinyl alcohol, polyacrylic acid, polyamines, and similar additives.
  • the zinc electrode can further include materials that improve its performance, for example zirconia fibers in the amount 0.5%-7%.
  • the current collector of the zinc electrode can be produced from copper, copper alloys, nickel, nickel alloys, lead, lead alloys, steel, stainless steel, bismuth, bismuth alloys, tin, tin alloys, zinc and zinc alloys, silver and silver alloys, carbon, graphite, expanded graphite, graphene, composites of graphite materials.
  • the current collector can be covered by an additional layer to increase conductivity, to protect from corrosion, to improve mechanical, chemical or physical properties as required by the system.
  • the material of an additional layer can include zinc, tin, lead indium, bismuth, antimony, nickel, silver or their alloys.
  • the ratio of the components of the alloys can be selected from interval from 0.1% to 99.9%. In certain special cases the content of an additive can be lower than 0.1%.
  • the third component can be added if required.
  • Said metal layer can be deposited by electroplating, electroless plating, hot metallization, painting, and liquid metal pulverization.
  • the current collector can be processed by rolling, casting, expanding, printing, stamping.
  • zinc (or its alloy with lead, 1 mass %,) can be casted at temperature 550° C. to form a grid.
  • Another approach is to roll zinc sheet to thickness about 0.5 mm, then slit the sheet into strips of 1 mm width, then cast zinc again locally to unite the strips in one current collector.
  • Such a current collector is lighter than a current collector formed completely by casting by about 30%-50%.
  • the current collector of this invention is covered by a layer of zinc-copper-bismuth alloy, which improves long term stability of the current collector.
  • the composition includes 15%-35% of bismuth, 0.5%-5% of copper and the rest is zinc.
  • the alloy is deposited by electrochemical or chemical plating or casting.
  • a current collector made of brass can be covered with zinc-copper-bismuth alloy by deepening the basic current collector into alloy at 490° C.
  • Nickel electrode of the battery can be produced starting from nickel hydroxide of the battery grade that includes, for example, cobalt and zinc additives in amount from 1 to 10 percent.
  • Nickel hydroxide is mixed with nickel powder, for example T255 of Novamet corporation, which is added in the amount 1%-20% by weight; about 0.5%-5% of ptfe dispersion is included as a binder, a 0.5%-4% of hydroxymethylcellulose is added to improve wetability.
  • the mixture is turned into paste by adding water or electrolyte, and rubbed into nickel foam electrode.
  • both electrodes are mounted into battery, and reduced by continuous or pulse current with the amount of passed electricity exceeding theoretical by about 10%-50%. If the zinc electrode is made of zinc powder composition, the nickel electrode is charged in a separate electrochemical cell to be compatible with the charged zinc electrode.
  • the current collector of the nickel-oxide hydroxide electrode is produced from nickel, titanium, stainless steel, cobalt, lead, and alloys of mentioned metals.
  • the current collector can be formed from mesh, foam, corrugated metal sheet, or expanded metal.
  • a current collector for a wall mounted nickel electrode is produced as a composite electrode, which is foil on one side and foam on the other.
  • This invention proposes current collectors for nickel-zinc and zinc-air batteries with one side as continued sheet, while on the other as foam, expanded metal, mesh or other high surface area material.
  • the composite current collectors can be formed from one metal, for example nickel, or two different materials, for example nickel and stainless steel.
  • the foam portion can be made from carbon foam.
  • the current collector can be produced by welding (including ultrasonic and laser welding), gluing, soldering, pressing, rolling, electrochemical plating, electrochemical etching (on the high surface area side), chemical etching, or pulverization with subsequent thermal treatment.
  • Electrolyte for nickel-zinc and zinc-air batteries is formulated on the basis KOH, NaOH, LiOH or mixture thereof. Typical electrolyte mass concentrations in water, or mixture of water with organic solvent is in the interval 10%-40%.
  • the increase of the battery life by replacement of the zinc cartridge can be accomplished in a zinc-air battery where the zinc electrode is low cost, and has short cycle life, while the air reduction and oxygen evolution electrodes have long lifetime.
  • Two air electrodes, one for air reduction, and another for oxygen evolution, eliminate the use of a bifunctional rechargeable air electrode, and increase lifetime of both air electrodes.
  • a three electrode zinc-air storage device does not require any adjustment of the red-ox state of the zinc electrode because two air electrodes include only a layer of a catalyst. For this reason the zinc cartridge in the zinc-air battery works like a fuel of a fuel cell.
  • a zinc-air battery with replaceable and rechargeable zinc cartridges can be considered as a hybrid of a rechargeable battery and a fuel cell.
  • the design of the three electrode zinc-air cell can be similar to nickel-zinc cell illustrated in FIG. 1 .
  • the air reduction electrode will take place of the nickel electrode 1
  • oxygen evolution electrode will be placed instead of plastic wall 2 .
  • the base 6 and zinc electrode cartridge are the same as in the nickel-zinc battery.
  • the oxygen evolution electrode includes at least a gas evolution catalyst layer, and a hydrophobic layer exposed to air.
  • the hydrophobic layer is formed from hydrophobic carbons, nitride materials, (for example boron nitride,) ptfe or polysilicon rubbers.
  • the current collector is made of nickel, nickel alloys, stainless steel, lead, manganese dioxide or their alloys or compositions.
  • the catalyst for oxygen evolution can be selected from iridium oxide, ruthenium oxide, or composition of these materials, mixture or chemical compositions based on nickel cobalt oxides, manganese dioxide or other oxygen evolution catalysts know in the field.
  • Oxygen reduction electrode includes at least catalyst layer, and hydrophobic layer exposed to air.
  • the composition of the hydrophobic layer is similar to the composition of the hydrophobic layer of the oxygen evolution electrode, while oxygen reduction electrode can include catalysts for oxygen reduction such as manganese dioxide, nickel cobalt oxides, nitrogen doped carbon, iron, cobalt or their complexes deposited on carbon, graphene, and expanded graphite.
  • the difference between nickel-zinc and zinc-air battery is in the charge-discharge voltage.
  • the zinc-air battery is discharged at about 1.0V-1.25V depending on current, while nickel-zinc battery is discharged at 1.65V.
  • the nickel-zinc battery can be charged at 1.7V-1.8V while the zinc-air battery at 1.95V-2.3V.
  • the efficiency of recharge of the zinc-air battery can be increased when the zinc oxide electrode is reduced in a separate cell with a counter electrode (electroactive substrate) different from water.
  • organic or inorganic substrates which oxidation can be performed at essentially lower potentials than water oxidation, and the regeneration efficiency can be effectively increased.
  • An example of such a substrate is chlorine that can be oxidized at potentials lower than the potential of water oxidation to oxygen.
  • zinc, air and oxygen evolution electrodes are substances, which are used as electrode components of supercapacitors.
  • examples of such a materials include carbon black, N-doped carbon materials, graphene, lead, tin, copper, iron, nickel, bismuth, silver powders; conducting polymers: polyaniline, polythiophene, polypyrrole and their derivatives; manganese oxides, nickel oxides, cobalt oxides, lead oxide, ruthenium oxide, iridium oxide, silver oxide, and compositions/alloys of these materials.
  • oxygen evolution electrodes often include ruthenium and iridium dioxides catalysts, which are also materials for supercapacitors.
  • a zinc-air battery which includes high surface area carbon materials, has embedded supercapacitance that can influence the shape of the charge-discharge curves.
  • An example of a charge-discharge characteristic of a zinc-air battery with extra capacitance is provided in FIG. 9 .
  • Charge-discharge profile is modified by sharp current peaks that appeared after voltage switch from charge to discharge and vise-versa. This effect can be very helpful in many applications.
  • the zinc-air battery often requires a supercapacitor connected in parallel to the battery.
  • the addition of a supercapacitor can increase weight/volume ratio, and the price of the storage device.
  • the internal supercapacitance can raise temporal power capabilities without any increase in the weight, volume and price of the device. It is important to note that supercapacitor properties are inherent to the electrodes of a zinc-air battery, and appear to a certain degree as intrinsic property of a metal-air battery irrespective of intention to use them.
  • the cells can be united in the modules as is shown in FIG. 2 .
  • the module is produced as the whole part; the module is not assembled from cells.
  • a base is formed from two parts. One of them is shown in FIG. 4 .
  • This part includes grooves 10 that form channels in the base.
  • the second part is similar to that shown in the FIG. 4 , however can be produced without grooves. Both components are joined using ultrasonic welding to form module base.
  • the shape of the module base shown in FIG. 4 is very convenient for automated production by milling, 3d printing, casting, injection molding and similar techniques.
  • the module is made of plastic like polyethylene, polypropylene, polybutylene, polyacrylate, silicone rubber, or ceramic.
  • the module can be assembled from elemental cells as a flexible component by connecting the cells with flexible tubes as shown in FIG. 3 . If flexible tubes are connected to the channels formed inside the base, as described above, the tubes can be filled with the electrolyte, and the whole battery can have one electrolyte level.
  • the flexible module attached to the backside of a jacket can be used to build a wearable battery.
  • FIG. 4 shows a base for two cells
  • FIG. 3 demonstrates the module assembled from three cells. The same principle can be applied to a module with any reasonable number and sizes of the elemental cells.
  • the internal channels can also be used to produce a nickel-zinc or zinc-air flow battery. A flow zinc battery has extended cycle life about 2000 cycles. In case of the zinc-air or nickel-zinc flow battery the flow of electrolyte is used for electrolyte cleaning.
  • “smart ABS” can be applied as module case material. ABS can be processed by most conventional low cost 3d printers. Smart ABS is a variety of ABS with melting temperature about 10° C. higher than ABS. FIG. 5 demonstrates a fragment of the base printed using “smart ABS” and conventional 3d printer. In addition to the formation of the groove 10 the printer fills the internal space of the case with honeycombs 12 . This makes the case about 50% lighter than conventional one. The decrease of weight can be also achieved by adding empty microspheres or hollow fibers. The example of hollow fibers is alumina and zirconia fibers available on market.
  • Nickel-zinc or zinc-air modules can be assembled in batteries using rotational joints as presented in FIGS. 6A and 6B .
  • the zinc modules can be replaced without disassembling the batteries as shown in FIG. 6C .
  • FIG. 6 shows a battery made of three modules, however any reasonable number of modules can be used.
  • a battery made of four cells is used as an example.
  • Me, OR and OE of FIG. 7 are metal, oxygen reduction, and oxygen evolution electrodes correspondingly.
  • a set of relays are shown on the right side of FIG. 7 . Each relay, when off, connects the metal and the air reduction electrodes, and the battery can be discharged without outside control.
  • Zinc electrode current collector (4 cm*6 cm) has been produced by deposition of the Zn—Bi—Cu alloy with mass content 80% Zn, 20% Bi and 5% Cu on brass mesh 40 at 550° C.
  • Electroactive zinc composition was prepared by mixing 8.1 g of zinc dust, 5 mkm size, 0.2 g of lead oxide, 0.2 g of m-aminodiphenylamine, 0.2 g zirconia hollow fibers, 0.2 g of ptfe dispersion, 0.1 g of carboxymethylcellulose with water. The mixture is deposited on brass current collector and wrapped into cellophane separator. The separator is sealed using double scotch.
  • Nickel electrode of the same size is prepared by welding nickel foam (pore diameters 0.3 mm-0.7 mm) to the nickel sheet 0.2 mm thickness; mixing 8.1 g of nickel oxide-hydroxide that includes 2% of ZnO and 5% of CoO with 1.5 g nickel powder, 0.2 g ptfe dispersion, 0.1 g carboxymethylcellulose; adding water and mixing, rubbing the composition into the foam part of the current collector.
  • the nickel hydroxide electrode was electrochemically oxidized at 100 mA/cm 2 current in 30% KOH against nickel sheet counter electrode to produce nickel oxide-hydroxide electrode.
  • the base is formed by milling a pocket in 0.25′′ thick polypropylene sheet.
  • the nickel electrode and polypropylene sheet of 1/16 in thickness were glued to the base.
  • the zinc cartridge was placed into the case between the nickel electrode and the plastic wall.
  • the cell was filled with 30% KOH 5% LiOH solution.
  • the cell was closed with the rubber plug, sealed by polysilicone liquid rubber, and dried at room temperature.
  • the battery has been discharged at 31 load and 1.65V for three hours, and charged at 1.75V-1.8V for the same time.
  • the zinc cartridge could be replaced by deleting the cartridge together with the rubber plug, removing the old zinc electrode, installing a new one, moving the cartridge with rubber plug into the cell, and sealing the cell with polysilicone rubber.
  • This example demonstrates assembling a module of three cell zinc-air battery, which is presented in FIG. 8 .
  • Three zinc cartridges have been produced similar to Example 1.
  • the base of the module for three cells was assembled from two parts.
  • One of the base sheets made of polypropylene was milled to produce the cell pockets and groves as shown in FIG. 4 .
  • Another base sheet was produced with pockets, but without grooves. Both sheets were glued with polyethylene based hot melt glue.
  • the air electrode catalyst was prepared by mixing 12 g of acid treated carbon black with 0.1 g-mol of m-phenylenediamine in 100 mL of 0.5M HCl solution. 0.05 g-mol ammonium persulfate and 0.05 g-mol FeCl 3 were added to solution at 10° C. and mixed for 24 h. Produced precursor was dried, and heat treated at 800° C. for 1 h. Then the sample was leached in 0.5M H 2 SO 4 at 80° C. for 5 h, washed and heat treated at 800° C. for 1 h again.
  • Three current collectors (4 cm*6 cm) were assembled by welding nickel mesh 40 to nickel foam.
  • the air electrode catalyst was rubbed into nickel foam part of the electrode.
  • the electrode was covered with a hydrophilic layer made from composition of ptfe dispersion in water and carbon black. This dispersion was mixed, and applied in form of 1 mm layer to the nickel current collector with the catalyst.
  • the air electrode had been heat treated at 320° C. for 3 min.
  • Three current collectors for the air evolution electrodes were assembled from stainless steel mesh 100.
  • the catalyst layer of RuO 2 was deposited by anodic oxidation of stainless steel 304 electrode in 1M HCl solution, and 0.01M solution of (NH 4 ) 2 RuCl 6 at 0.9V vs Ag/AgCl reference electrode for 30 min.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Power Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Microelectronics & Electronic Packaging (AREA)
  • Sustainable Energy (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Hybrid Cells (AREA)

Abstract

Rechargeable and replaceable zinc cartridges have been used as the components of nickel-zinc batteries. The battery life of a zinc battery is extended by periodic replacing of the zinc anodes at about 10% of the battery cost. Flat modules that include several cells interconnected with channels are used as basic elements of a flat battery. A home wall battery is produced by assembling the modules using rotational joints. The performance of the zinc current collectors is improved by deposition of Zn—Cu—Bi alloy. Zinc composition is formulated using additives of polyphenylenediamines and zirconium hollow fibers.

Description

  • This application claims benefit to U.S. provisional application No. 62/044,666 filed Sep. 2, 2014, and to US provisional application No 6207926 filed Nov. 13, 2014, and to U.S. provisional application No. 62/167,581 filed May 28, 2015 all of the subject matter has been incorporated by reference.
  • This work was supported by National Research Council—Industrial Research Assistance Program, Project No 829964, 2014.
    • FIELD OF THE INVENTION
  • This invention proposes thin (˜1 cm) home wall energy storage devices based on zinc-air and nickel-zinc batteries with replaceable and rechargeable zinc modules.
    • BACKGROUND OF THE INVENTION
  • Energy storage devices are key components of future economy. Zinc batteries, which are low cost, high energy and safe to operate, are prospective storage devices for reserve power, electric grid, and transportation.
  • Batteries for homes recently received special attention: at the end of April 2015 Tesla Motors offered 10 KWh, 2 KW batteries of 130 cm×86 cm×18 cm size. These batteries have been advertised as wall mounted. The batteries had moderate power capabilities about 2 KW. Lithium batteries with higher performance (for example 1 KWh battery with 1 KW power) are essentially more expensive with prices in the range $600/KWh-$900/KWh.
  • Batteries with nickel oxide-hydroxide cathodes (also referred as nickel cathodes) are attractive because of long cycle life of the nickel electrode. Linden's Handbook of Batteries specifies lifetime of nickel-cadmium batteries as 8-25 years. The cadmium electrode has been phasing out from mass production because of safety concerns. Nickel-metal hydride batteries that have replaced nickel-cadmium storage devices are more expensive that nickel-cadmium batteries.
  • The commercialization of large-sized nickel-zinc rechargeable batteries is appealing because of relatively high discharge voltage 1.65V, low cost, safety, and high power capabilities. Nickel-zinc batteries have 30% higher energy density in comparison with nickel-metal hydride devices. A nickel-zinc battery with the cost about $300/KWh and power capabilities of a lithium battery, ten years lifetime, and 5,000-7,500 charge-discharge cycles can be considered as effective substitute for large-sized lithium batteries.
  • Zinc-air batteries are the cheapest (based on cost per energy density) batteries at market, and allows very high specific energies up to 280 Wh/kg. Rechargeable zinc-air batteries have two basic designs: a) batteries with bifunctional air-electrodes, and b) batteries with dual air electrodes. In case of dual air electrodes one electrode is used for air reduction while another one for oxygen evolution. In case of rechargeable batteries with dual air electrodes the growth of metal dendrites is localized between metal and oxygen evolution electrodes. As the result no dendrites appear at the interface between zinc and oxygen reduction electrodes what eliminates short circuits during discharge. The use of dual air electrodes allows better selection and optimization of current collectors as well as catalysts to insure better cycle life of the storage devices.
  • An example of a battery with dual air electrode is described by Tzidon et al in WO Pat. No. 2012/156872 A1. This battery has six electrodes: two zinc, two air (reduction), and two oxygen evolution electrodes. A metal-air battery assembled from elemental cells is arranged face-to-face, and requires leaving air gaps about 1 mm-2 mm to allow air access to the whole surface of the air electrode. Taking into account that the thickness of an elemental cell is about (or less) than 10 mm, the presence of air gaps increases battery volume by 10%-20%. Rechargeable batteries with zinc anodes have cycle life about 500-900 cycles.
  • The objectives of this invention are as follows:
      • a) To propose design and method of operation of a nickel-zinc battery that increases its lifetime and cycle life
        • To suggest module design for cells with replaceable and rechargeable zinc anodes
      • b) To design a wall mounted battery that allows replacing rechargeable zinc anodes without disassembling the battery
      • c) To improve the design of a replaceable and rechargeable zinc cartridge.
    BRIEF DESCRIPTION OF THE INVENTION
  • This invention uses rechargeable and replaceable zinc cartridges as components of nickel-zinc batteries. The cycle life of the batteries can be increased by replacing zinc cartridges at about 10% of the battery cost. As the result the total lifetime of the anode can be extended to be compatible with that of the nickel-oxide hydroxide cathode. It is suggested a flat design of the modules interconnected with channels as basic elements of wall mounted batteries. The home wall battery design includes rotational joints to assure zinc cartridge replacement without disassembling the batteries.
  • The design of the zinc cartridges is improved by using current collectors covered with Zn—Cu—Bi alloy. Zinc composition is formulated using additives of polyphenylenediamines and zirconium hollow fibers. A flat module with battery/supercapacitor characteristics has been demonstrated.
    • BRIEF DESCRIPTION OF THE DRAWINGS
  • FIG. 1 shows horizontal cross section of a nickel-zinc cell with replaceable and rechargeable zinc anodes. The cell includes the nickel oxide hydroxide electrode 1, the cell wall 2, the zinc anode 3, the electrolyte 4, the separator 5 and the base 6. An individual cell is specified as 7.
  • FIG. 2 demonstrates a flat module made of the cells 7.
  • FIG. 3 illustrates a foldable module where the cells 7 are joined with the flexible tubes 8.
  • FIG. 4 displays a portion of the module base with pockets 9, grooves 10; and connection holes 11.
  • FIG. 5 demonstrates a portion of the module base printed by a 3d printer; the picture shows grooves 10, and honeycomb structure 12.
  • FIG. 6A shows the front view of a wall mounted battery assembled from three modules connected using rotational joints 13. FIG. 6B shows the side view of the wall mounted battery with rotational joints 13. FIG. 6C shows the side view of the wall mounted battery where joints 13 are rotated to replace zinc anodes 3.
  • FIG. 7 shows an example of a circuit that commutates three cells. Each cell includes an oxygen reduction (OR), metal (Me) and oxygen evolution (OE) electrodes, multiple relays with control contacts 14; the circuit also includes switch 15, and optional resistor 16.
  • FIG. 8 shows practical implementation of a zinc-air module made of three cells, and controlled by a dual three position relay 17.
  • FIG. 9 shows cycling profile of a zinc-air module made of three cells
    •  DETAILED DESCRIPTION OF THE INVENTION
  • Low cost rechargeable zinc cartridges are intended to be used as the components of the nickel-zinc battery. After degradation an old zinc cartridge is replaced by a new one at about 10% of the battery cost to serve the next period. As the result the capital cost of the battery is increased by 10% for the second period, but not by 100% when the battery is replaced completely.
  • The specific of the design is a flat low cost plastic cell, and a module assembled by gluing, ultrasonic welding, heat treatment, or plastic welding. FIG. 1 shows horizontal cross section of a nickel-zinc cell with replaceable zinc anode. The cell includes the nickel oxide hydroxide electrode 1, the cell wall 2, the zinc anode 3, the electrolyte 4, the separator 5 and the base 6. The cell can include two nickel anodes fixed as the cell walls.
  • A replaceable zinc cartridge is formed of zinc electrode 3 that includes a current collector and zinc electrode composition, and sealed with separator envelop 4. The thickness of the cartridge is selected in such a way that it fits free space (pocket) of the cell, and can be moved out of the cell without any physical or functional damage to the electrode. Typical thickness of the zinc cartridge is in the interval from 0.1 mm to 1 cm. The cartridges with lower/larger thickness will also work, but might be unpractical. The idea of a replaceable electrode is applicable to any other rechargeable electrode that can be used with nickel-metal and metal-air batteries. For example a replaceable and rechargeable anode can be formed from iron, cobalt, cadmium, nickel hydride, or the alloys of metals. On the other hand the idea can be applied to other batteries like silver-zinc battery if a high cycle life silver electrode is available.
  • The replacement of the zinc cartridge can be performed when the battery (and the nickel electrode) is discharged. In this case a new zinc electrode, which replaces old one, should be also in the discharged state. This can be achieved by formulation of the zinc electrode on the basis of doped zinc oxide and additives. A zinc electrode formed from zinc powder can be chemically or electrochemically discharged before moving into discharged nickel-zinc battery. The zinc cartridge can also be replaced when the nickel electrode is in the charged state; in this case a charged zinc electrode is used to complement the state of charge of the nickel electrode.
  • Zinc cartridge includes a zinc electrode wrapped in the separator, or in the anion-exchange membrane. The separator/membrane envelope is hermetically sealed, so that ions can exchange with electrolyte solely through the separator or membrane or a combination thereof. Separator is made from a porous material stable in alkaline solutions. Examples of separator materials include polyethylene, polypropylene, and cellophane. Such a porous material can include a thin layer of an anion exchange material.
  • The zinc electrode can be formed from zinc powder, or zinc oxide doped with lead, bismuth, indium, aluminum or other metals that inhibit hydrogen evolution during charging. Zinc or zinc oxide paste can also include carboxymethylcellulose, polyvinyl alcohol, polyacrylic acid, polyamines, and similar additives. The zinc electrode can further include materials that improve its performance, for example zirconia fibers in the amount 0.5%-7%.
  • The current collector of the zinc electrode can be produced from copper, copper alloys, nickel, nickel alloys, lead, lead alloys, steel, stainless steel, bismuth, bismuth alloys, tin, tin alloys, zinc and zinc alloys, silver and silver alloys, carbon, graphite, expanded graphite, graphene, composites of graphite materials. The current collector can be covered by an additional layer to increase conductivity, to protect from corrosion, to improve mechanical, chemical or physical properties as required by the system. The material of an additional layer can include zinc, tin, lead indium, bismuth, antimony, nickel, silver or their alloys. The ratio of the components of the alloys can be selected from interval from 0.1% to 99.9%. In certain special cases the content of an additive can be lower than 0.1%. The third component can be added if required. Said metal layer can be deposited by electroplating, electroless plating, hot metallization, painting, and liquid metal pulverization.
  • The current collector can be processed by rolling, casting, expanding, printing, stamping. For example zinc, (or its alloy with lead, 1 mass %,) can be casted at temperature 550° C. to form a grid. Another approach is to roll zinc sheet to thickness about 0.5 mm, then slit the sheet into strips of 1 mm width, then cast zinc again locally to unite the strips in one current collector. Such a current collector is lighter than a current collector formed completely by casting by about 30%-50%.
  • The current collector of this invention is covered by a layer of zinc-copper-bismuth alloy, which improves long term stability of the current collector. The advantage of the mentioned alloy over other alloys its low toxicity and flexibility. The composition includes 15%-35% of bismuth, 0.5%-5% of copper and the rest is zinc. The alloy is deposited by electrochemical or chemical plating or casting. For example a current collector made of brass can be covered with zinc-copper-bismuth alloy by deepening the basic current collector into alloy at 490° C.
  • Nickel electrode of the battery can be produced starting from nickel hydroxide of the battery grade that includes, for example, cobalt and zinc additives in amount from 1 to 10 percent. Nickel hydroxide is mixed with nickel powder, for example T255 of Novamet corporation, which is added in the amount 1%-20% by weight; about 0.5%-5% of ptfe dispersion is included as a binder, a 0.5%-4% of hydroxymethylcellulose is added to improve wetability. The mixture is turned into paste by adding water or electrolyte, and rubbed into nickel foam electrode.
  • When the anode is made of zinc oxide composition, both electrodes (nickel hydroxide and zinc oxide) are mounted into battery, and reduced by continuous or pulse current with the amount of passed electricity exceeding theoretical by about 10%-50%. If the zinc electrode is made of zinc powder composition, the nickel electrode is charged in a separate electrochemical cell to be compatible with the charged zinc electrode.
  • The current collector of the nickel-oxide hydroxide electrode is produced from nickel, titanium, stainless steel, cobalt, lead, and alloys of mentioned metals. The current collector can be formed from mesh, foam, corrugated metal sheet, or expanded metal. A current collector for a wall mounted nickel electrode is produced as a composite electrode, which is foil on one side and foam on the other.
  • This invention proposes current collectors for nickel-zinc and zinc-air batteries with one side as continued sheet, while on the other as foam, expanded metal, mesh or other high surface area material. The composite current collectors can be formed from one metal, for example nickel, or two different materials, for example nickel and stainless steel. The foam portion can be made from carbon foam. The current collector can be produced by welding (including ultrasonic and laser welding), gluing, soldering, pressing, rolling, electrochemical plating, electrochemical etching (on the high surface area side), chemical etching, or pulverization with subsequent thermal treatment.
  • Electrolyte for nickel-zinc and zinc-air batteries is formulated on the basis KOH, NaOH, LiOH or mixture thereof. Typical electrolyte mass concentrations in water, or mixture of water with organic solvent is in the interval 10%-40%.
  • The increase of the battery life by replacement of the zinc cartridge can be accomplished in a zinc-air battery where the zinc electrode is low cost, and has short cycle life, while the air reduction and oxygen evolution electrodes have long lifetime. Two air electrodes, one for air reduction, and another for oxygen evolution, eliminate the use of a bifunctional rechargeable air electrode, and increase lifetime of both air electrodes. Unlike nickel-zinc battery, a three electrode zinc-air storage device does not require any adjustment of the red-ox state of the zinc electrode because two air electrodes include only a layer of a catalyst. For this reason the zinc cartridge in the zinc-air battery works like a fuel of a fuel cell. A zinc-air battery with replaceable and rechargeable zinc cartridges can be considered as a hybrid of a rechargeable battery and a fuel cell.
  • The design of the three electrode zinc-air cell can be similar to nickel-zinc cell illustrated in FIG. 1. In case of the zinc-air battery the air reduction electrode will take place of the nickel electrode 1, while oxygen evolution electrode will be placed instead of plastic wall 2. The base 6 and zinc electrode cartridge are the same as in the nickel-zinc battery.
  • The oxygen evolution electrode includes at least a gas evolution catalyst layer, and a hydrophobic layer exposed to air. The hydrophobic layer is formed from hydrophobic carbons, nitride materials, (for example boron nitride,) ptfe or polysilicon rubbers. The current collector is made of nickel, nickel alloys, stainless steel, lead, manganese dioxide or their alloys or compositions. The catalyst for oxygen evolution can be selected from iridium oxide, ruthenium oxide, or composition of these materials, mixture or chemical compositions based on nickel cobalt oxides, manganese dioxide or other oxygen evolution catalysts know in the field.
  • Oxygen reduction electrode includes at least catalyst layer, and hydrophobic layer exposed to air. The composition of the hydrophobic layer is similar to the composition of the hydrophobic layer of the oxygen evolution electrode, while oxygen reduction electrode can include catalysts for oxygen reduction such as manganese dioxide, nickel cobalt oxides, nitrogen doped carbon, iron, cobalt or their complexes deposited on carbon, graphene, and expanded graphite.
  • The difference between nickel-zinc and zinc-air battery is in the charge-discharge voltage. The zinc-air battery is discharged at about 1.0V-1.25V depending on current, while nickel-zinc battery is discharged at 1.65V. The nickel-zinc battery can be charged at 1.7V-1.8V while the zinc-air battery at 1.95V-2.3V. As the result the recharging efficiency of the nickel-zinc battery is higher about 0.8-0.85 when the same characteristic of a zinc-air battery is about 0.5-0.65 depending on the effectiveness of oxygen reduction and oxygen evolution catalysts. The efficiency of recharge of the zinc-air battery can be increased when the zinc oxide electrode is reduced in a separate cell with a counter electrode (electroactive substrate) different from water.
  • There is a line of organic or inorganic substrates, which oxidation can be performed at essentially lower potentials than water oxidation, and the regeneration efficiency can be effectively increased. An example of such a substrate is chlorine that can be oxidized at potentials lower than the potential of water oxidation to oxygen.
  • Many components of the zinc, air and oxygen evolution electrodes are substances, which are used as electrode components of supercapacitors. Examples of such a materials include carbon black, N-doped carbon materials, graphene, lead, tin, copper, iron, nickel, bismuth, silver powders; conducting polymers: polyaniline, polythiophene, polypyrrole and their derivatives; manganese oxides, nickel oxides, cobalt oxides, lead oxide, ruthenium oxide, iridium oxide, silver oxide, and compositions/alloys of these materials.
  • On one hand mentioned substances can accumulate extra charge at the border with electrolyte electrostatically. On the other hand these materials can function as catalysts or conducting additives of the metal-air batteries. For example, oxygen evolution electrodes often include ruthenium and iridium dioxides catalysts, which are also materials for supercapacitors.
  • A zinc-air battery, which includes high surface area carbon materials, has embedded supercapacitance that can influence the shape of the charge-discharge curves. An example of a charge-discharge characteristic of a zinc-air battery with extra capacitance is provided in FIG. 9. Charge-discharge profile is modified by sharp current peaks that appeared after voltage switch from charge to discharge and vise-versa. This effect can be very helpful in many applications.
  • To meet temporal power requirements of an application, the zinc-air battery often requires a supercapacitor connected in parallel to the battery. The addition of a supercapacitor can increase weight/volume ratio, and the price of the storage device. The internal supercapacitance can raise temporal power capabilities without any increase in the weight, volume and price of the device. It is important to note that supercapacitor properties are inherent to the electrodes of a zinc-air battery, and appear to a certain degree as intrinsic property of a metal-air battery irrespective of intention to use them.
  • The cells can be united in the modules as is shown in FIG. 2. In fact the module is produced as the whole part; the module is not assembled from cells. First of all a base is formed from two parts. One of them is shown in FIG. 4. This part includes grooves 10 that form channels in the base. The second part is similar to that shown in the FIG. 4, however can be produced without grooves. Both components are joined using ultrasonic welding to form module base. The shape of the module base shown in FIG. 4 is very convenient for automated production by milling, 3d printing, casting, injection molding and similar techniques. The module is made of plastic like polyethylene, polypropylene, polybutylene, polyacrylate, silicone rubber, or ceramic. The module can be assembled from elemental cells as a flexible component by connecting the cells with flexible tubes as shown in FIG. 3. If flexible tubes are connected to the channels formed inside the base, as described above, the tubes can be filled with the electrolyte, and the whole battery can have one electrolyte level. The flexible module attached to the backside of a jacket can be used to build a wearable battery.
  • Two types of nickel-zinc batteries can be assembled: sealed batteries similar to conventional nickel batteries, and batteries that have no conventional sealing. Latter can lose humidity slowly because of evaporation. The internal channels of the module, and flexible tubes make electrolyte common for all cells. The compensation (preferably automated) of the evaporated electrolyte is processed using one opening for the whole battery. FIG. 4 shows a base for two cells, FIG. 3 demonstrates the module assembled from three cells. The same principle can be applied to a module with any reasonable number and sizes of the elemental cells. The internal channels can also be used to produce a nickel-zinc or zinc-air flow battery. A flow zinc battery has extended cycle life about 2000 cycles. In case of the zinc-air or nickel-zinc flow battery the flow of electrolyte is used for electrolyte cleaning.
  • According to this invention “smart ABS” can be applied as module case material. ABS can be processed by most conventional low cost 3d printers. Smart ABS is a variety of ABS with melting temperature about 10° C. higher than ABS. FIG. 5 demonstrates a fragment of the base printed using “smart ABS” and conventional 3d printer. In addition to the formation of the groove 10 the printer fills the internal space of the case with honeycombs 12. This makes the case about 50% lighter than conventional one. The decrease of weight can be also achieved by adding empty microspheres or hollow fibers. The example of hollow fibers is alumina and zirconia fibers available on market.
  • Nickel-zinc or zinc-air modules can be assembled in batteries using rotational joints as presented in FIGS. 6A and 6B. In this case the zinc modules can be replaced without disassembling the batteries as shown in FIG. 6C. FIG. 6 shows a battery made of three modules, however any reasonable number of modules can be used.
  • It is obvious that in case of three electrode zinc-air batteries a switch is required to transfer the battery made of several elemental cells from charge to discharge mode. The solution offered in this invention is based on the circuit shown in FIG. 7.
  • A battery made of four cells is used as an example. Me, OR and OE of FIG. 7 are metal, oxygen reduction, and oxygen evolution electrodes correspondingly. A set of relays are shown on the right side of FIG. 7. Each relay, when off, connects the metal and the air reduction electrodes, and the battery can be discharged without outside control.
  • To charge the battery, voltage from a power supply is applied to the battery, and to the relays circuit control by turning the switch 15 “on”. An optional resistance 16 can be used to decrease voltage in correspondence with the relay specifications.
    • EXAMPLES OF PRACTICAL IMPLEMENTATION Example 1
  • This example demonstrates a flat nickel-zinc battery designed with a wall mounted nickel-oxide hydroxide electrode, and a replaceable zinc cartridge. Zinc electrode current collector (4 cm*6 cm) has been produced by deposition of the Zn—Bi—Cu alloy with mass content 80% Zn, 20% Bi and 5% Cu on brass mesh 40 at 550° C. Electroactive zinc composition was prepared by mixing 8.1 g of zinc dust, 5 mkm size, 0.2 g of lead oxide, 0.2 g of m-aminodiphenylamine, 0.2 g zirconia hollow fibers, 0.2 g of ptfe dispersion, 0.1 g of carboxymethylcellulose with water. The mixture is deposited on brass current collector and wrapped into cellophane separator. The separator is sealed using double scotch.
  • Nickel electrode of the same size is prepared by welding nickel foam (pore diameters 0.3 mm-0.7 mm) to the nickel sheet 0.2 mm thickness; mixing 8.1 g of nickel oxide-hydroxide that includes 2% of ZnO and 5% of CoO with 1.5 g nickel powder, 0.2 g ptfe dispersion, 0.1 g carboxymethylcellulose; adding water and mixing, rubbing the composition into the foam part of the current collector. The nickel hydroxide electrode was electrochemically oxidized at 100 mA/cm2 current in 30% KOH against nickel sheet counter electrode to produce nickel oxide-hydroxide electrode.
  • The base is formed by milling a pocket in 0.25″ thick polypropylene sheet. The nickel electrode and polypropylene sheet of 1/16 in thickness were glued to the base. The zinc cartridge was placed into the case between the nickel electrode and the plastic wall. The cell was filled with 30% KOH 5% LiOH solution. The cell was closed with the rubber plug, sealed by polysilicone liquid rubber, and dried at room temperature. The battery has been discharged at 31 load and 1.65V for three hours, and charged at 1.75V-1.8V for the same time. The zinc cartridge could be replaced by deleting the cartridge together with the rubber plug, removing the old zinc electrode, installing a new one, moving the cartridge with rubber plug into the cell, and sealing the cell with polysilicone rubber.
    • Example 2
  • This example demonstrates assembling a module of three cell zinc-air battery, which is presented in FIG. 8. Three zinc cartridges have been produced similar to Example 1. The base of the module for three cells was assembled from two parts. One of the base sheets made of polypropylene was milled to produce the cell pockets and groves as shown in FIG. 4. Another base sheet was produced with pockets, but without grooves. Both sheets were glued with polyethylene based hot melt glue.
  • The air electrode catalyst was prepared by mixing 12 g of acid treated carbon black with 0.1 g-mol of m-phenylenediamine in 100 mL of 0.5M HCl solution. 0.05 g-mol ammonium persulfate and 0.05 g-mol FeCl3 were added to solution at 10° C. and mixed for 24 h. Produced precursor was dried, and heat treated at 800° C. for 1 h. Then the sample was leached in 0.5M H2SO4 at 80° C. for 5 h, washed and heat treated at 800° C. for 1 h again.
  • Three current collectors (4 cm*6 cm) were assembled by welding nickel mesh 40 to nickel foam. The air electrode catalyst was rubbed into nickel foam part of the electrode. The electrode was covered with a hydrophilic layer made from composition of ptfe dispersion in water and carbon black. This dispersion was mixed, and applied in form of 1 mm layer to the nickel current collector with the catalyst. The air electrode had been heat treated at 320° C. for 3 min. Three current collectors for the air evolution electrodes were assembled from stainless steel mesh 100. The catalyst layer of RuO2 was deposited by anodic oxidation of stainless steel 304 electrode in 1M HCl solution, and 0.01M solution of (NH4)2RuCl6 at 0.9V vs Ag/AgCl reference electrode for 30 min. Then hydrophobic layers were deposited on the top of the catalyst layers similar to that of the air electrodes. Then three air reduction electrodes, and three oxygen evolution electrodes have been glued to the base using hot melt glue to form three cells. Three zinc electrodes were placed in the pockets, and sealed with liquid polysilicone rubber similar to the nickel-zinc battery of Example 1. Then a circuit, similar to presented in FIG. 7 was assembled. The difference was in the number of cells, and the type of the relay; the circuit for redesigned to accommodate three cells, and a dual relay replaced two single relays. The three cell battery could be discharged at 3Ω resistor, and charged with voltage 6.7V.

Claims (28)

1. A battery cell, other than metal-air battery, that includes a zinc anode with current collector, a cathode with current collector, and electrolyte wherein the zinc anode is rechargeable and replaceable
2. A battery cell of claim 1 wherein the cathode is nickel oxide-hydroxide
3. Rechargeable and replaceable zinc anode of claim 1 wherein the zinc anode is wrapped in a hermetically sealed separator
4. Rechargeable and replaceable zinc anode of claim 1 wherein the zinc anode includes zinc powder or dust with particle sizes in the interval 0.1 mkm-7 mkm
5. Rechargeable and replaceable zinc anode of claim 1 wherein the zinc anode includes polyaminodiphenylamine, or its derivative in concentration range 0.1%-7%
6. Rechargeable and replaceable zinc anode of claim 1 wherein the zinc anode includes current collector made of zinc, nickel, copper, bronze, stainless steel, lead, bismuth or their alloys covered with a layer of zinc-bismuth-copper alloy
7. A current collector of a nickel-oxide hydroxide, an air reduction, an oxygen evolution electrodes wherein the current collector is made of low surface area material on one side, and large surface area material on the other side
8. A current collector of claim 7 wherein large surface area material is metal foam
9. A current collector of claim 7 wherein low surface area material is metal sheet, foil, mesh or expanded metal
10. A battery module that includes a base, two walls, a cathode, as well as rechargeable and replaceable zinc anodes wherein the module is flat, and is internally connected with channels filled with electrolyte
11. A battery module of claim 10 wherein the module base is formed of two sheets with pockets for zinc electrodes
12. A battery module of claim 10 wherein the module includes walls made of nickel oxide-hydroxide cathodes
13. A module of claim 10 wherein the module includes walls made of air reduction and oxygen evolution electrodes
14. A module of claim 10 wherein the module is a hybrid of a battery and a supercapacitor
15. A module of claim 10 wherein the module is assembled by gluing
16. A module of claim 10 wherein the module case is made of “smart ABS” plastic formed by 3d printing or casting
17. A module of claim 10 wherein the module case is made of plastic, rubber, or ceramic filled with empty spheres or hollow fibers
18. A module of claim 10 wherein the module is split into elemental cells connected to each other with flexible tubes
19. A module of claim 10 wherein the module is split into elemental cells connected to each other with flexible tubes filled with electrolyte
20. A home wall mounted battery wherein the battery is formed of flat modules that include rechargeable and replaceable zinc anodes, and is assembled using rotational joints
21. A method of operation of batteries with replaceable and rechargeable zinc anodes wherein the anodes are replaced periodically after a long term interval
22. A method of operation of batteries of claim 21 wherein the zinc anodes are replaced with discharged zinc anodes when the cathodes are in the discharged state
23. A method of operation of batteries of claim 21 wherein the zinc anodes are replaced with charged zinc anodes when the cathodes are in the charged state
24. A method of production of the battery module with rechargeable and replaceable zinc anodes wherein
a) Two polymer sheets are milled to form the pockets for elemental cells
b) The channels are milled in one or the both sheets
c) The sheets are glued, welded to each other to form the base of the module
d) Nickel oxide-hydroxide cathodes and plastic sheets are glued to the base to form side walls
e) The replaceable and rechargeable zinc electrodes are placed in the pockets
f) The pockets are closed with rubber or plastic caps
g) The caps are sealed with a sealant
25. The method of claim 24 wherein at stage d) the air evolution and air reduction electrodes are glued to the module base
26. A battery module of claim 10 wherein the electrodes are connected using three position relays, and by default the module is in the discharge mode of operation
27. A battery module of claim 10 wherein the electrodes are connected using three position relays in such a way that the connection to the charger turns the relays to charging mode
28. Rechargeable and replaceable zinc anode of claim 1 wherein the zinc anode includes zirconia hollow fibers in the amount 0.1%-5% mass %
US14/840,020 2014-09-02 2015-08-30 Wall Mounted Zinc Batteries Abandoned US20160204441A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US14/840,020 US20160204441A1 (en) 2014-09-02 2015-08-30 Wall Mounted Zinc Batteries
US15/081,885 US10608243B2 (en) 2014-09-02 2016-03-26 Batteries with replaceable zinc cartridges

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US201462044666P 2014-09-02 2014-09-02
US201562167581P 2015-05-28 2015-05-28
US14/840,020 US20160204441A1 (en) 2014-09-02 2015-08-30 Wall Mounted Zinc Batteries

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US15/081,885 Division US10608243B2 (en) 2014-09-02 2016-03-26 Batteries with replaceable zinc cartridges

Publications (1)

Publication Number Publication Date
US20160204441A1 true US20160204441A1 (en) 2016-07-14

Family

ID=56368160

Family Applications (2)

Application Number Title Priority Date Filing Date
US14/840,020 Abandoned US20160204441A1 (en) 2014-09-02 2015-08-30 Wall Mounted Zinc Batteries
US15/081,885 Expired - Fee Related US10608243B2 (en) 2014-09-02 2016-03-26 Batteries with replaceable zinc cartridges

Family Applications After (1)

Application Number Title Priority Date Filing Date
US15/081,885 Expired - Fee Related US10608243B2 (en) 2014-09-02 2016-03-26 Batteries with replaceable zinc cartridges

Country Status (1)

Country Link
US (2) US20160204441A1 (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110600746A (en) * 2019-09-24 2019-12-20 河南超力新能源有限公司 Composite current collector for zinc-based battery, preparation method of composite current collector, negative plate and zinc-based battery
CN110828855A (en) * 2019-11-07 2020-02-21 上海电力大学 Flexible self-oxygen-supply rechargeable zinc-air battery pack module
CN111509306A (en) * 2020-04-26 2020-08-07 河北大学 Electrolyte for rechargeable zinc ion battery, preparation method of electrolyte and rechargeable zinc ion battery
US20210351458A1 (en) * 2020-05-07 2021-11-11 Zelos Energy Ltd. Space Configurable Battery Structures For Electrode Assemblies Incorporating Ion Exchange Materials
US11228053B2 (en) * 2019-05-17 2022-01-18 Nextech Batteries, Inc. Pouch cell battery including an ion exchange membrane
WO2022027474A1 (en) * 2020-08-06 2022-02-10 东莞新能安科技有限公司 Battery
WO2022082168A1 (en) * 2020-10-14 2022-04-21 Uop Llc Mixed metal manganese oxide material
US20220246920A1 (en) * 2021-01-29 2022-08-04 Hunt Energy Enterprises, L.L.C. Anode for zn-based batteries
CN116097479A (en) * 2020-04-28 2023-05-09 泽洛斯能源有限公司 Polymer coating method for electrode assembly including ion exchange material
CN117542948A (en) * 2024-01-10 2024-02-09 华北电力大学 Aqueous zinc-ion battery negative electrode material, preparation method and zinc-ion battery
US20240363869A1 (en) * 2022-01-10 2024-10-31 Henan Chaoli New Energy Co., Ltd. Preparation methods of composite current collectors for zinc secondary batteries, negative electrode plates, and zinc secondary batteries

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102032184B1 (en) * 2016-12-21 2019-10-18 재단법인 포항산업과학연구원 METAL FOIL SUPPORTED ELECTRODE AND Zn-Ni FLOW SECONDARY BATTERY COMPRISING THE SAME

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5554918A (en) * 1994-03-08 1996-09-10 Electric Fuel (E.F.L.) Ltd. Mechanically-rehargeable battery
US6617072B2 (en) * 2001-11-27 2003-09-09 Ovonic Battery Company, Inc. Positive active electrode composition with graphite additive
US20060231487A1 (en) * 2005-04-13 2006-10-19 Bartley Stuart L Coated filter media
US20130143127A1 (en) * 2010-07-30 2013-06-06 Hitachi Chemical Company, Ltd. Anode material for lithium ion secondary battery, anode for lithium ion secondary battery, and lithium ion secondary battery
US20140147757A1 (en) * 2012-11-28 2014-05-29 The Government of the United States of America, as represented by the Ssecretary of the Navy Zinc electrodes for batteries

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4246324A (en) * 1979-04-09 1981-01-20 Diamond Shamrock Technologies S.A. Consumable replaceable anodes for batteries
US4804448A (en) * 1987-06-24 1989-02-14 Eltron Research, Inc. Apparatus for simultaneous generation of alkali metal species and oxygen gas
FR2624526B1 (en) * 1987-12-14 1992-04-30 Ricoh Kk COMPOSITE ELECTRODE COMPRISING AN ALUMINUM BODY LINKED TO AN ELECTRICALLY CONDUCTIVE POLYMER AND ELECTRIC CELL USING SUCH A COMPOSITE ELECTRODE
CA2110097C (en) * 1992-11-30 2002-07-09 Soichiro Kawakami Secondary battery
CN1145231C (en) * 1997-01-28 2004-04-07 佳能株式会社 Electrode structure, rechargeable battery and manufacturing method thereof
US7112389B1 (en) * 2005-09-30 2006-09-26 E. I. Du Pont De Nemours And Company Batteries including improved fine fiber separators
WO2008099288A2 (en) 2007-02-16 2008-08-21 Vyro Games Ltd. Biosensor device and method
US20100062347A1 (en) * 2008-09-09 2010-03-11 Lin-Feng Li Rechargeable zinc cell with longitudinally-folded separator

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5554918A (en) * 1994-03-08 1996-09-10 Electric Fuel (E.F.L.) Ltd. Mechanically-rehargeable battery
US6617072B2 (en) * 2001-11-27 2003-09-09 Ovonic Battery Company, Inc. Positive active electrode composition with graphite additive
US20060231487A1 (en) * 2005-04-13 2006-10-19 Bartley Stuart L Coated filter media
US20130143127A1 (en) * 2010-07-30 2013-06-06 Hitachi Chemical Company, Ltd. Anode material for lithium ion secondary battery, anode for lithium ion secondary battery, and lithium ion secondary battery
US20140147757A1 (en) * 2012-11-28 2014-05-29 The Government of the United States of America, as represented by the Ssecretary of the Navy Zinc electrodes for batteries

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11228053B2 (en) * 2019-05-17 2022-01-18 Nextech Batteries, Inc. Pouch cell battery including an ion exchange membrane
CN110600746A (en) * 2019-09-24 2019-12-20 河南超力新能源有限公司 Composite current collector for zinc-based battery, preparation method of composite current collector, negative plate and zinc-based battery
CN110828855A (en) * 2019-11-07 2020-02-21 上海电力大学 Flexible self-oxygen-supply rechargeable zinc-air battery pack module
CN111509306A (en) * 2020-04-26 2020-08-07 河北大学 Electrolyte for rechargeable zinc ion battery, preparation method of electrolyte and rechargeable zinc ion battery
CN116097479A (en) * 2020-04-28 2023-05-09 泽洛斯能源有限公司 Polymer coating method for electrode assembly including ion exchange material
US11831000B2 (en) * 2020-05-07 2023-11-28 Zelos Energy Ltd. Space configurable battery structures for electrode assemblies incorporating ion exchange materials
US20210351458A1 (en) * 2020-05-07 2021-11-11 Zelos Energy Ltd. Space Configurable Battery Structures For Electrode Assemblies Incorporating Ion Exchange Materials
WO2022027474A1 (en) * 2020-08-06 2022-02-10 东莞新能安科技有限公司 Battery
WO2022082168A1 (en) * 2020-10-14 2022-04-21 Uop Llc Mixed metal manganese oxide material
US20220246920A1 (en) * 2021-01-29 2022-08-04 Hunt Energy Enterprises, L.L.C. Anode for zn-based batteries
US20240363869A1 (en) * 2022-01-10 2024-10-31 Henan Chaoli New Energy Co., Ltd. Preparation methods of composite current collectors for zinc secondary batteries, negative electrode plates, and zinc secondary batteries
US12347869B2 (en) * 2022-01-10 2025-07-01 Henan Chaoli New Energy Co., Ltd. Preparation methods of composite current collectors for zinc secondary batteries, negative electrode plates, and zinc secondary batteries
CN117542948A (en) * 2024-01-10 2024-02-09 华北电力大学 Aqueous zinc-ion battery negative electrode material, preparation method and zinc-ion battery

Also Published As

Publication number Publication date
US10608243B2 (en) 2020-03-31
US20160351890A1 (en) 2016-12-01

Similar Documents

Publication Publication Date Title
US20160204441A1 (en) Wall Mounted Zinc Batteries
CN114551984B (en) Solid state bipolar battery with thick electrodes
Besenhard Handbook of battery materials
US10910674B2 (en) Additive for increasing lifespan of rechargeable zinc-anode batteries
US8945756B2 (en) Composite anode structure for aqueous electrolyte energy storage and device containing same
KR102166391B1 (en) Secondary zinc-manganese dioxide batteries for high power applications
EP2238063B1 (en) Elevator backup system
CN107093773A (en) Battery
CA2841558A1 (en) High voltage battery composed of anode limited electrochemical cells
KR20150027085A (en) Lithium ion capacitor
KR20140005976A (en) Battery electrode and battery
EP3951983A1 (en) Metal plating-based electrical energy storage cell
WO2020086835A1 (en) A protective barrier layer for alkaline batteries
JP5557385B2 (en) Energy storage device with proton as insertion species
JP6945788B2 (en) Rechargeable batteries, battery packs, vehicles, stationary power supplies and negative electrodes
EP3300146B1 (en) Metal-ion secondary battery
WO2002059986A2 (en) Electrode with flag-shaped tap
CN109119635B (en) Battery with a battery cell
CN117154011A (en) Sulfide impregnated columnar silicon anode for all-solid-state battery and method of forming the same
Loupe et al. Electrochemical energy storage: current and emerging technologies
EP3089244B1 (en) Aluminium-manganese oxide electrochemical cell
CN114284548A (en) Battery cell of all-solid-state battery, all-solid-state battery and electronic equipment
CN222801854U (en) A hybrid internal series battery cell, battery and electrical equipment
Dell Aqueous electrolyte batteries
JP2021082383A (en) Negative electrode for zinc battery

Legal Events

Date Code Title Description
STPP Information on status: patent application and granting procedure in general

Free format text: NON FINAL ACTION MAILED

STPP Information on status: patent application and granting procedure in general

Free format text: RESPONSE TO NON-FINAL OFFICE ACTION ENTERED AND FORWARDED TO EXAMINER

STPP Information on status: patent application and granting procedure in general

Free format text: FINAL REJECTION MAILED

STPP Information on status: patent application and granting procedure in general

Free format text: ADVISORY ACTION MAILED

STPP Information on status: patent application and granting procedure in general

Free format text: DOCKETED NEW CASE - READY FOR EXAMINATION

STPP Information on status: patent application and granting procedure in general

Free format text: AWAITING RESPONSE FOR INFORMALITY, FEE DEFICIENCY OR CRF ACTION

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION