US20190036179A1 - Electrochemical cell with getter and method of forming same - Google Patents

Electrochemical cell with getter and method of forming same Download PDF

Info

Publication number
US20190036179A1
US20190036179A1 US16/049,535 US201816049535A US2019036179A1 US 20190036179 A1 US20190036179 A1 US 20190036179A1 US 201816049535 A US201816049535 A US 201816049535A US 2019036179 A1 US2019036179 A1 US 2019036179A1
Authority
US
United States
Prior art keywords
electrode
electrochemical cell
bis
borate
imide
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
US16/049,535
Inventor
Craig Downie
Robert Ellis Doe
David Eaglesham
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.)
Viking Power Systems Pte Ltd
Original Assignee
PELLION TECHNOLOGIES Inc
Pellion Technologies
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 PELLION TECHNOLOGIES Inc, Pellion Technologies filed Critical PELLION TECHNOLOGIES Inc
Priority to US16/049,535 priority Critical patent/US20190036179A1/en
Assigned to PELLION TECHNOLOGIES INC. reassignment PELLION TECHNOLOGIES INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: DOE, ROBERT ELLIS, DOWNIE, CRAIG, EAGLESHAM, DAVID
Publication of US20190036179A1 publication Critical patent/US20190036179A1/en
Assigned to VIKING POWER SYSTEMS PTE. LTD reassignment VIKING POWER SYSTEMS PTE. LTD ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: PELLION TECHNOLOGIES, INC.
Priority to US17/200,041 priority patent/US20210218080A1/en
Abandoned legal-status Critical Current

Links

Images

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/52Removing gases inside the secondary cell, e.g. by absorption
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01DCOMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
    • C01D15/00Lithium compounds
    • C01D15/02Oxides; Hydroxides
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/056Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0564Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
    • H01M10/0566Liquid materials
    • H01M10/0567Liquid materials characterised by the additives
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/058Construction or manufacture
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/362Composites
    • H01M4/366Composites as layered products
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/449Separators, membranes or diaphragms characterised by the material having a layered structure
    • H01M50/451Separators, membranes or diaphragms characterised by the material having a layered structure comprising layers of only organic material and layers containing inorganic material
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/449Separators, membranes or diaphragms characterised by the material having a layered structure
    • H01M50/454Separators, membranes or diaphragms characterised by the material having a layered structure comprising a non-fibrous layer and a fibrous layer superimposed on one another
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/056Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0564Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
    • H01M10/0566Liquid materials
    • H01M10/0568Liquid materials characterised by the solutes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/056Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0564Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
    • H01M10/0566Liquid materials
    • H01M10/0569Liquid materials characterised by the solvents
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0025Organic electrolyte
    • H01M2300/0028Organic electrolyte characterised by the solvent
    • H01M2300/0037Mixture of solvents
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Definitions

  • the disclosure generally relates to electrochemical cells. More particularly, exemplary embodiments of the present disclosure relate to electrochemical cells including a getter.
  • Electrochemical cells such as rechargeable or secondary electrochemical cells, can be used to power a variety of devices, such as mobile phones, portable computers, other portable devices, electric or hybrid cars, as well as many other appliances.
  • electrochemical cells with relatively high energy density (energy that can be derived from a cell per unit volume of the cell), relatively high specific energy density (energy that can be derived per unit weight of the cell or per unit weight of the active electrode material), and/or relatively high average discharge potential of the cell, so that desired energy can be supplied to a device using the cell, while minimizing the mass and/or volume of the cell.
  • electrochemical cells include an anode, a cathode, a separator between the anode and cathode, and an electrolyte.
  • an oxidation-reduction reaction occurs, causing electrons flow, through an external circuit, from the anode to the cathode, and cations are attracted from the anode to the cathode.
  • the cells can be recharged by causing electrons and cations to flow in the opposite direction using a charger.
  • electrochemical cells particularly of high-energy electrochemical cells (e.g., electrochemical cells with an average discharge potential of 3.5 Volts or more)
  • undesired reactions of one or more components within an electrochemical cell e.g., between one or more components of the electrolyte and/or between one or more components within an electrolyte and one or more components of an anode and/or a cathode
  • one or more of electrolyte components can oxidize or otherwise degrade to form unwanted gas.
  • the produced gas can cause an increase in the cell volume, thereby reducing the energy density of the cell, can cause a reduction of the capacity of the electrochemical cell, can deleteriously affect other discharge performance of the cell, and/or can be a safety hazard.
  • getter material that is sealed apart from the electrochemical cell has been used to capture gas, such as carbon dioxide formed within an electrochemical cell.
  • gas such as carbon dioxide formed within an electrochemical cell.
  • placing a seal between the getter material and the electrochemical cell can add undesired weight and/or volume to the electrochemical cell and can prevent the getter material from addressing gas production during regular charging and discharging of the electrochemical cell.
  • U.S. Pat. No. 4,448,860 in the name of von Lanka et al., discloses a cell that is protected against the danger of corrosion of the alkali metal electrode, particularly due to moisture penetrating from the outside the cell, by providing the cell with a gas-absorbing getter material.
  • the gas-absorbing getter material is designed to mitigate danger associated with in-flowing ambient oxygen, CO 2 , or inwardly diffusing water.
  • the reference does not disclose techniques for addressing gasses that form as a result of high-energy cell operation.
  • U.S. Pat. No. 7,776,465 in the name of Hatazawa et al., discloses a battery that includes an outer covering member that includes a laminated film and battery element (electrochemical cell) contained within the outer covering member and sealed therein.
  • the outer covering member includes a gas absorbable material interposed between the outermost layer of the outer covering member and the battery element.
  • the gas-absorbable material is not part of the electrochemical cell, but rather is separated from the electrochemical cell and included in an outer covering member.
  • U.S. Pat. No. 8,460,808 in the name of Toia et al., discloses a rechargeable battery that includes means for sorbing harmful substances.
  • the means includes a polymeric housing that is permeable to said harmful substances but impermeable to the electrolyte.
  • One or more getter materials for the sorption of said harmful substances are included within the polymeric housing.
  • U.S. Pat. No. 8,834,180 in the name of Woo et al., discloses a secondary battery that includes an electrode assembly, a gas-collecting member, and a battery case.
  • the electrode assembly includes first and second electrode plates and a separator interposed between the first and second electrode plates.
  • the gas-collecting member is provided separately and adjacent to the electrode assembly.
  • the battery case encases the electrode assembly and the gas-collecting member.
  • U.S. Pat. No. 9,114,382 in the name of Visconti et al., discloses a carbon dioxide composite getter that includes an envelope that is permeable to CO 2 and powders of a first and a second active material contained within the envelope.
  • the first active material is lithium hydroxide and the second active material is lithium oxide.
  • the getter is separate from the electrochemical cell, and thus adds significant volume to a battery.
  • electrochemical cells suffers various drawbacks. Accordingly, improved electrochemical cells including getter material, batteries including the electrochemical cells, and methods of forming the same are desired.
  • Various embodiments of the present disclosure provide improved electrochemical cells including getter material, including one or more gas getters, in direct contact with one or more components of the electrochemical cells—i.e., the getter material or getters are not contained in a separate envelope or container. This allows the getter(s) to work efficiently, without adding significant weight or volume to the cells or batteries including the cells.
  • Use of getters in direct contact with one or more components of the electrochemical cell can also efficiently capture gas that forms within the cell (e.g., within an electrolyte of the cell) during use and/or facilitate high voltage operation of the cells.
  • an electrochemical cell such as a secondary or rechargeable electrochemical cell, includes a first electrode, a second electrode, a separator between the first electrode and the second electrode, a non-aqueous electrolyte, and a getter material comprising one or more gas getters (also referred to herein simply as getter or getters), wherein the one or more gas getters are in direct contact with, form part of, or both one or more of the first electrode, the second electrode, the separator, and the non-aqueous electrolyte.
  • the non-aqueous electrolyte comprises a salt that does not readily hydrolyze.
  • the one or more salts do not comprise an anion selected from the group consisting of PF 6 ⁇ 1 , BF 4 ⁇ 1 , AlCl 4 ⁇ 1 , AsF 6 ⁇ 1 , ClO 4 ⁇ 1 , SiF 6 ⁇ 1 , or SbF 6 ⁇ 1 .
  • Exemplary salts suitable for use in exemplary electrolytes comprise at least three elements and include two or more of the following: boron, phosphorous, fluorine, carbon, nitrogen, sulfur, and oxygen.
  • Non-limiting examples of exemplary salts of the disclosure include use of one or more salts comprise one or more anions selected from the group consisting of triflate (CF 3 SO 3 ⁇ 1 ), triflinate (CF 3 SO 2 ⁇ 1 ), perfluorobutanesulfonate (C 4 F 9 SO 3 ⁇ 1 ), bis(perfluoroalkylsulfonyl)imide [N((C x F 2x+1 ) x SO 2 ) 2 ⁇ 1 ], bis(trifluoromethane) sulfonimide [N(CF 3 SO 2 ) 2 ⁇ 1 ], bis(perfluoroethylsulfonyl)imide [N(C 2 F 5 SO 2 ) 2 ⁇ 1 ], bis(fluorosulfonyl)imide [N(SO 2 F) 2 ⁇ 1 ], bis(perfluoropinacolato)borate [B(C 6 F 12 O 2 ) 2 ⁇ 1 ], bis(oxal
  • the one or more salts include a cation, such as lithium.
  • the electrochemical cell is a high-energy rechargeable electrochemical cell with having an average discharge potential of ⁇ 3.5 V, ⁇ 4 V, ⁇ 4.25 V, or ⁇ 4.5 V.
  • the electrochemical cell is a high-energy rechargeable electrochemical cell having an upper charge cutoff potential of ⁇ 4.3 V, ⁇ 4.35 V, ⁇ 4.4 V, or ⁇ 4.45 V.
  • the electrolyte can be a fluid, such as a liquid or a gel, which may also be in contact with solid ion conductors at least incorporated into the cell electrolyte in part (e.g., polymer, glass, ceramic).
  • the first electrode can include Li, Li alloys such as Si, Sn, Bi, Al, Li 4 Ti 5 O 12 , hard carbon, graphitic carbon, and amorphous carbon.
  • the second electrode can include second electrode active material, such as transition metal oxides, transition metal oxo-anions, chalcogenides, halogenides and combinations thereof.
  • transition metal oxides comprised of one or more transition metals and one or more redox active transition metals such as Lithium Cobalt Oxide, Lithium Nickel Manganese Cobalt Oxide, and Lithium Nickel Cobalt Aluminum Oxide compositions.
  • Non-limiting examples of positive electrode active materials for the Li battery include Lithium metal phosphates and tavorites such as LiFePO 4 , Lithium metal oxide spinels LiMn 2 O 4 , and Li NASICON's Li 3 V 2 (PO 4 ) 3 .
  • the separator can include, for example, porous polypropylene, porous polyethylene, aramid fiber, or glass fiber.
  • the one or more gas getters can include at least one of a metal oxide and a metal hydroxide, such as one or more compounds selected from the group consisting of: LiOH, Li 2 O, NaOH, Na 2 O, KOH, K 2 O, Mg(OH) 2 , MgO, Ca(OH) 2 , and CaO in any combination.
  • the getter material can further include one or more of carbon, polymer, resin, metal, or ceramic in any combination.
  • the getter material does not include any of a silica gel, an alumina, or a zeolite.
  • the getter material can be included as part of a coating that is applied to one or more of the first electrode, the second electrode, and the separator. Additionally or alternatively, the getter material can be incorporated into one or more of the first electrode, the second electrode, the separator, and the electrolyte.
  • a composite getter includes one or more gas getters or gas getter materials (e.g., as described herein) dispersed in a non-aqueous fluid.
  • the gas getter(s) and/or getter material(s) can be dispersed in a non-aqueous fluid as a mixture, suspension, or colloid.
  • the non-aqueous fluid can include one or more (e.g., lithium) salts that do not readily hydrolyze or dissolve in the one or more non-aqueous solvents.
  • the one or more salts do not comprise an anion selected from the group consisting of PF 6 ⁇ 1 , BF 4 ⁇ 1 , AlCl 4 ⁇ 1 , AsF 6 ⁇ 1 , ClO 4 ⁇ , SiF 6 ⁇ 1 , or SbF 6 ⁇ 1 .
  • the one or more salt may not include the one or more salts do not comprise any of LiPF 6 , LiBF 4 , LiAlCl 4 , LiAsF 6 , LiClO 4 , LiSiF 6 , or LiSbF 6 .
  • the non-aqueous fluid comprises one or more salts of at least one of the following anions: triflate (CF 3 SO 3 ⁇ 1 ), triflinate (CF 3 SO 2 ⁇ 1 ), perfluorobutanesulfonate (C 4 F 9 SO 3 ⁇ 1 ), bis(perfluoroalkylsulfonyl)imide [N((C x F 2x+1 ) x SO 2 ) 2 ⁇ 1 ], bis(trifluoromethane) sulfonimide [N(CF 3 SO 2 ) 2 ⁇ 1 ], bis(perfluoroethylsulfonyl)imide [N(C 2 F 5 SO 2 ) 2 ⁇ 1 ], bis(fluorosulfonyl)imide [N(SO 2 F) 2 ⁇ 1 ], bis(perfluoropinacolato) borate [B(C 6 F 12 O 2 ) 2 ⁇ 1 ], bis(oxalato)bor
  • the one or more salts comprise at least three elements and include two or more of the following: boron, phosphorous, fluorine, carbon, nitrogen, sulfur, and oxygen.
  • the non-aqueous fluid can include at least one solvent that is a non-aqueous polar aprotic solvent.
  • the non-aqueous fluid comprises at least one solvent including: ethers, organic carbonates, tertiary amines, lactones, ketones, glymes, nitriles, ionic liquids, aliphatic and aromatic hydrocarbon solvents, and organic nitro solvents.
  • the non-aqueous fluid comprises at least one solvent including THF, 2-methyl THF, dimethoxyethane, diglyme, triglyme, tetraglyme, diethoxyethane, diethylether, proglyme, ethyl diglyme, butyl diglyme, fluorinated ether, hydrofluoroethers, ethylene carbonate, fluoro-ethylene carbonate, dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate, dimethylsulfoxide, dimethylsulfite, sulfolane, ethyl methyl sulfone, acetonitrile, hexane, toluene, fluoro-toluene, nitromethane, 1-3 dioxalane, 1-3 dioxane, 1-4 dioxane, trimethyl phosphate, tri-ethyl phosphate, hexa-methyl-phosphoramide (HM
  • a concentration of the salt, or a combination of the one or more salts in the non-aqueous fluid ranges from, for example, about 0.01 M to about 10 M.
  • the composite getter can be incorporated into one or more components of an electrochemical device, such as the electrochemical cells, and batteries described herein.
  • the composite getter can be or be incorporated into a coating that is applied to one or more of electrodes, packaging material, and the insulating separator of the electrochemical cell.
  • the electrochemical cell or device can be configured to charge to, for example, greater than or equal to 4.0 V or other voltages described herein.
  • a battery includes one or more electrochemical cells as described herein.
  • the batteries can additionally include a casing and/or one or more leads.
  • Exemplary batteries can be in the form of coin battery, a soft pack cell laminate, a cylindrical cell, or the like.
  • a method of forming an electrochemical cell includes the steps of forming a structure comprising a first electrode, a second electrode, and a separator between the first and second electrodes, and providing a getter material in direct contact with one or more of the first electrode, the second electrode, and the separator, and the electrolyte.
  • the method can include introducing a mixture, solution, colloid, or suspension of getter material and a liquid to the structure, wherein the getter material directly contacts one or more of the first electrode, the second electrode, and the separator, removing at least a portion of the liquid, and after removing at least a portion of the liquid, adding an electrolyte solution to the structure.
  • a battery can be formed by adding a casing around the electrochemical cell.
  • the liquid employed to introduce the getter material as a mixture, solution, colloid, or suspension include water, alcohol, ester, ketone, ether, lactam, amide, nitrile, methanol, ethanol, isopropanol, carbonate, ethyl methyl carbonate, dimethyl carbonate, tetrahydrofuran, 1, 2-dimethoxy ethane, acetone, N-methyl-2-pyrrolidone, and acetonitrile.
  • FIG. 1 illustrates an electrochemical cell in accordance with at least one exemplary embodiment of the disclosure.
  • FIG. 2 illustrates another electrochemical cell in accordance with at least one exemplary embodiment of the disclosure.
  • FIG. 3 illustrates a battery in accordance with at least one exemplary embodiment of the disclosure.
  • FIG. 4 illustrates a typical voltage profile for a cell containing a getter in intimate contact with an electrode assembly and a non-aqueous electrolyte (darker line) as compared to the same cell construction without the getter (lighter line).
  • FIG. 5 illustrates the mass loss for a set of 4.5 Ah cells containing a getter in intimate contact with the electrode assembly and non-aqueous electrolyte (A) as compared to the same cell construction without the getter (B).
  • FIG. 6 illustrates the mass loss for 5 Ah cells containing a getter in intimate contact with an electrode assembly and non-aqueous electrolyte (C) as compared to the same cell construction without the getter (D).
  • FIG. 7 illustrates a typical voltage profile for a cell containing a getter coated upon an electrode surface in intimate contact with non-aqueous electrolyte (darker line) as compared to the same cell construction without the getter (lighter line).
  • any ranges indicated may include or exclude the endpoints. Any values of variables indicated (regardless of whether they are indicated with “about” or not) may refer to precise values or approximate values and include equivalents, and may refer to average, median, representative, majority, or a single value.
  • electrochemical cells that include a getter or getter material in direct contact with or that forms part of one or more components of an electrochemical cell that can form part of a battery.
  • Exemplary electrochemical cells described herein maintain a relatively high energy density, specific energy, and/or can operate at relatively high energy levels (e.g., average discharge voltages of ⁇ 3.5 V, ⁇ 4 V, ⁇ 4.25 V, or ⁇ 4.5 V).
  • the electrochemical cell is a high-energy rechargeable electrochemical cell having an upper charge cutoff potential of ⁇ 4.3 V, ⁇ 4.35 V, ⁇ 4.4 V, or ⁇ 4.45 V.
  • exemplary electrochemical cells are relatively safe, because the getter captures an amount of gas that is produced within a battery and therefore reduces a likelihood of battery rupture.
  • Examples of this disclosure can be used to form a variety of types of electrochemical cells. For illustration purposes, specific embodiments are described herein in the context of rechargeable, or secondary, lithium-based electrochemical cells such as lithium-ion electrochemical cells and rechargeable lithium metal cells, and those that combine attributes of both. However, the disclosure is not limited to such examples, unless otherwise noted.
  • Lithium-ion cells generally contain active materials that operate on the principle of intercalation wherein Li+ ions migrate in and out of host structures (e.g., graphitic negative electrodes and layered transition metal oxide positive electrode materials) without breaking and forming chemical bonds. Hence there is relatively little structural change (e.g., ⁇ 5% volume expansion) within the electrode materials, and therefore the cell. Generally, this provides a high degree of reversibility for the electrochemical reactions in the cell, with minimal reaction surface area; however it also limits the energy density of the electrode, and therefore the cell.
  • host structures e.g., graphitic negative electrodes and layered transition metal oxide positive electrode materials
  • a high degree of repeated and uncontrolled surface area change and/or high voltage can facilitate a greater degree of parasitic chemical reactions, resulting in deterioration of the cell, cycle life, power density, and margin for safe operation-thus offsetting gains in energy density. Furthermore, such parasitic reactions can results in formation of gaseous products due to parasitic reactions between electrolyte components and/or between electrolyte components and electrode surfaces. Electrochemical cells including a getter in contact with or that forms part of one or more of the electrochemical cell components can address these issues.
  • FIG. 1 illustrates an electrochemical cell 100 in accordance with exemplary embodiments of the disclosure.
  • Electrochemical cell 100 includes a first electrode 102 , a second electrode 104 , a separator 106 interposed between first electrode 102 and second electrode 104 , a fluid electrolyte 112 in contact with first and second electrodes 102 , 104 , and optionally includes one or more layers (e.g., coatings) 114 , 116 , including getter material.
  • electrochemical cell 100 can additionally or alternatively include getter material incorporated into one or more of first electrode 102 , second electrode 104 , separator 106 , and/or electrolyte 112 .
  • electrochemical cell 100 is illustrated with two layers 114 , 116 including getter material, as described in more detail below, electrochemical cells in accordance with the disclosure can include additional getter material layers, only one of layers 114 , 116 , or may not include either of layers 114 , 116 .
  • electrochemical cell 100 also includes a first current collector 108 in electrical contact with first electrode 102 and a second current collector 110 in contact with the second electrode.
  • First electrode 102 (also sometimes referred to herein as a negative electrode or anode) comprises a negative electrode active material that can accept cations.
  • negative electrode active material for lithium-based electrochemical cells include Li, Li alloys such as Si, Sn, Bi, and/or Al alloys, Li 4 Ti 5 O 12 , hard carbon, graphitic carbon, and/or amorphous carbon.
  • Non-limiting examples of negative electrode active material for other rechargeable electrochemical cells include, Mg, Na, Ca, and alloys thereof, hard carbon, graphitic carbon, and/or amorphous carbon.
  • most (e.g., greater than 90 wt % to all) of the anode active material can be initially included in a discharged second electrode 104 (also sometimes referred to herein as a positive electrode or cathode) when electrochemical cell 100 is initially made, so that the electrode active material forms part of first electrode 102 during a first charge of electrochemical cell 100 —thus providing for a rechargeable electrochemical cell wherein N/P ratio ⁇ 4. That is, a rechargeable cell wherein the capacity of the first electrode 102 , N, and the capacity of the second electrode 104 , P, are configured such that N/P is ⁇ 4.
  • First electrode 102 and second electrode 104 can further include one or more electronically conductive additives.
  • electronically conductive additives include carbon black, Super P®, C-NERGYTM Super C65, Ensaco® black, Ketjenblack®, acetylene black, synthetic graphite such as Timrex® SFG-6, Timrex® SFG-15, Timrex® SFG-44, Timrex® KS-6, Timrex® KS-15, Timrex® KS-44, natural flake graphite, carbon nanotubes, fullerenes, hard carbon, or mesocarbon microbeads.
  • First electrode 102 can include any combination of the one or more electronically conductive additives.
  • first electrode 102 and/or second electrode 104 further includes one or more polymer binders.
  • polymer binders include poly-vinylidene fluoride (PVdF), poly(vinylidene fluoride-co-hexafluoropropene) (PVdF-HFP), Polytetrafluoroethylene (PTFE), Kynar Flex® 2801, Kynar® Powerflex LBG, and Kynar® HSV 900, and Teflon®.
  • First electrode 102 and/or second electrode 104 can include any combination of the one or more polymer binders.
  • first electrode 102 is configured to provide >1000 mAh/cc.
  • Non-limiting exemplary techniques for forming such electrodes are described in U.S. Patent Publication No. 2016/0172661.
  • First electrode 102 can optionally include getter material, which includes one or more gas getters.
  • the one or more gas getters can comprise one or more compounds selected from the group consisting of metal oxides and metal hydroxides.
  • a molar ratio of the metal oxides:metal hydroxides can depend on desired characteristics of the getters.
  • the getter material can include more metal hydroxide(s) to increase a speed of gas absorption or more metal oxide(s) to increase a capacity to capture gas.
  • Exemplary getters include compounds selected from the group consisting of: LiOH, Li 2 O, NaOH, Na 2 O, KOH, K 2 O, Mg(OH) 2 , MgO, Ca(OH) 2 , and CaO, which can be combined in any combination, or be one compound from the group.
  • Exemplary molar ratios of metal oxide(s) to metal hydroxide(s) range from about 0 to about 1, about 0.5 to about 0.5, or about 1 to about 0.
  • getter material can include one or more of carbon, polymer, resin, metal, or ceramic, in any combination. Such additional material(s) can be used to, for example, facilitate incorporation of the getter into one or more components of an electrochemical cell (e.g., electrode, separator, or electrolyte) or coat getter material onto the one or more of the components.
  • getter material does not comprise any of a silica gel, an alumina, or a zeolite.
  • An amount of the one or more gas getter can be a molar ratio equivalent (about more—e.g., about two, five, or ten percent more) to the mols of gas (e.g., CO 2 , CO, H 2 S, NO 2 , SO 2 , H 2 O, H 2 , O 2 , C 2 H 4 , C 3 H 6 , C x H 4*x , hydrocarbons) expected to be produced during charging and/or discharging of electrochemical cell 100 .
  • gas e.g., CO 2 , CO, H 2 S, NO 2 , SO 2 , H 2 O, H 2 , O 2 , C 2 H 4 , C 3 H 6 , C x H 4*x , hydrocarbons
  • Second electrode 104 (as noted above, also sometimes referred to herein as a positive electrode or cathode) can include intercalation material.
  • intercalation materials include transition metal oxides, transition metal oxo-anions, chalcogenides, halogenides and combinations thereof.
  • Non-limiting examples of positive electrode active materials for the lithium electrochemical cells include lithium transition metal oxides comprised of one or more transition metals and one or more redox active transition metals such as lithium cobalt oxide, lithium nickel manganese cobalt oxide compositions, lithium nickel cobalt aluminum compositions, and lithium metal phosphates and tavorites such as LiFePO4, lithium metal oxide spinels LiMn 2 O 4 , and Li NASICON's Li 3 V 2 (PO 4 ) 3 .
  • lithium nickel manganese cobalt oxide “NMC” can include a variety of transition metal ratios and lithium excess.
  • Exemplary NMC ratios include, but are not limited to, Li[Ni 1/3 Mn 1/3 Co 1/3 ]O 2 or so-called “111”, Li[Ni 5/3 Mn 3/3 Co 2/3 ]O 2 or so-called “532”, Li[Ni 6/3 Mn 2/3 Co 2/3 ]O 2 or so-called “622”, Li[Ni 8/3 Mn 1/3 Co 1/3 ]O 2 or so-called “811” either with stoichiometric or excess lithium to transition metals.
  • second electrode 104 may comprise conversion, or displacement, reaction materials.
  • Non-limiting examples of conversion, or displacement reaction materials includes sulfur, metal nitrides, metal phosphides, metal sulfides, metal oxides, metal fluorides, metal chlorides such as FeF 3 , FeF 2 , NiF 2 , CO 3 O 4 , ZnF 2 , FeS 2 , Li 2 O and at least one metal, LiF and at least one metal,
  • second electrode 104 may comprise an organic, or polymeric electro-active material.
  • Non-limiting examples include quinones such as dimethoxy benzoquinone, poly-anthraquinone, graphene, graphene oxide.
  • second electrode 104 can initially include most or all of the active material for first electrode 102 . Similar to first electrode 102 , second electrode 104 can optionally include getter material as described herein.
  • At least one of the first electrode 102 and the second electrode 104 include a metal, an alloy, or an intermetallic compound. In accordance with additional or alternative exemplary embodiments, at least one of the first electrode 102 and the second electrode 104 include a material configured to undergo an insertion reaction, an alloying, an intercalation, a disproportionation, a conversion reaction, or any combination thereof.
  • Separator 106 electrically isolates the first electrode from the second electrode and is permeable to at least one mobile species which is redox-active at least one of the first electrode and the second electrode.
  • Exemplary materials suitable for separator 106 in accordance with embodiments of the disclosure include porous virgin or coated polyolefin, polypropylene, polyethylene, aramix fiber, and glass fiber. Separator 106 can optionally comprise the getter material in part or entirely as described herein.
  • Electrolyte 112 can be a fluid, e.g., a liquid or a gel electrolyte, which may also be in contact with solid ion conductors at least incorporated into the cell electrolyte in part (e.g., polymer, glass, ceramic). Electrolyte 112 generally includes a solvent and one or more salts. Electrolyte 112 can, in some cases, also include getter material as described herein.
  • a fluid e.g., a liquid or a gel electrolyte, which may also be in contact with solid ion conductors at least incorporated into the cell electrolyte in part (e.g., polymer, glass, ceramic).
  • Electrolyte 112 generally includes a solvent and one or more salts. Electrolyte 112 can, in some cases, also include getter material as described herein.
  • non-aqueous solvents are suitable for use in the electrolyte 112 .
  • Non-aqueous solvents can be used alone or in any suitable combination. Whether a solvent comprises a single non-aqueous composition or a plurality of non-aqueous compositions, for the purposes of further exposition, the non-aqueous solvent will be referred to as “the solvent” in the singular.
  • the solvent advantageously should provide appreciable solubility by coordination of the constituent inorganic salts of the electroactive metal.
  • suitable solvents include non-aqueous polar aprotic solvents, ethers, organic carbonates, and tertiary amines, and may also include, lactones, ketones, glymes, nitriles, ionic liquids, aliphatic and aromatic hydrocarbon solvents and organic nitro solvents.
  • suitable solvents include THF, 2-methyl THF, dimethoxyethane, diglyme, triglyme, tetraglyme, diethoxyethane, diethylether, proglyme, ethyl diglyme, butyl diglyme, fluorinated ether, hydrofluoroethers, ethylene carbonate, fluoro-ethylene carbonate, dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate, dimethylsulfoxide, dimethylsulfite, sulfolane, ethyl methyl sulfone, acetonitrile, hexane, toluene, fluoro-toluene, nitromethane, 1-3 dioxalane, 1-3 dioxane, 1-4 dioxane, trimethyl phosphate, tri-ethyl phosphate, hexa-methyl-phosphoramide (HMPA), N,N-propyl-methyl-methyl
  • Exemplary salts for electrolyte 112 do not readily hydrolyze.
  • salts that do not readily hydrolyze are salts that do not react with trace amounts (e.g., ⁇ 3000 ppm) water in a autocatalytic decomposition reaction to form significant amounts (e.g., more than 300 ppm) of strong acid such as HF or HCl.
  • the one or more salts do not comprise an anion selected from the group consisting of PF 6 ⁇ 1 , BF 4 ⁇ 1 , AlCl 4 ⁇ 1 , AsF 6 ⁇ 1 , ClO 4 ⁇ 1 , SiF 6 ⁇ 1 , or SbF 6 ⁇ 1 .
  • Salts including such anions are thought to be susceptible to hydrolysis.
  • the one or more salts do not include any of LiPF 6 , LiBF 4 , LiAlCl 4 , LiAsF 6 , LiClO 4 , LiSiF 6 , or LiSbF 6 .
  • Exemplary compounds suitable for the one or more salts comprise at least three elements and include two or more of the following: boron, phosphorous, fluorine, carbon, nitrogen, and oxygen.
  • Non-limiting examples of exemplary salts of the disclosure include use of one or more salts comprise one or more anions selected from the group consisting of triflate (CF 3 SO 3 ⁇ 1 ), triflinate (CF 3 SO 2 ⁇ 1 ), perfluorobutanesulfonate (C 4 F 9 SO 3 ⁇ 1 ), bis(perfluoroalkylsulfonyl)imide [N((C x F 2x+1 ) x SO 2 ) 2 ⁇ 1 ], bis(trifluoromethane)sulfonimide [N(CF 3 SO 2 ) 2 ⁇ 1 ], bis(perfluoroethylsulfonyl)imide [N(C 2 F 5 SO 2 ) 2 ⁇ 1 ], bis(fluorosulfonyl)imide [N(SO 2 F) 2 ⁇ 1 ], bis(perfluoropinacolato) borate [B(C 6 F 12 O 2 ) 2 ⁇ 1 ], bis(oxala
  • the cation can be lithium, sodium, magnesium, or calcium.
  • a concentration of the salt, or a combination of salts in the electrolyte solution ranges from about 0.01 M to about 10 M, about 0.1 M to about 7 M, or about 0.25 to about 7 M, or from about 0.5 M to saturation.
  • non-aqueous fluid electrolyte comprising salts that do not readily hydrolyze permits the function of the gas getter material(s), and may in fact even expedite the gettering activity of such materials, while in intimate contact with the non-aqueous fluid electrolyte.
  • First current collector 108 and/or second current collector 110 can include any material capable of sufficiently conducting electrons.
  • Exemplary first/second electrode current collector 108 / 110 materials include aluminum, aluminum alloys, copper, copper alloys, nickel, nickel alloys, titanium, titanium alloys, steel, carbonaceous materials, and a metal substrate coated with an over-layer to prevent corrosion in the electrolyte.
  • FIG. 2 illustrates another electrochemical cell 200 in accordance with additional embodiments of the disclosure.
  • Electrochemical cell 200 is similar to electrochemical cell 100 , except electrochemical cell 200 includes a gate electrode 207 , in addition to the other cell components.
  • a circuit can be configured to measure an operating parameter of the device and to determine when a cell health event occurs and/or respond to the cell health event, as disclosed in U.S. Patent Publication No. 2016/0006081 in the name of Eaglesham et al., the contents of which are incorporated herein by reference, to the extent such contents do not conflict with the present disclosure.
  • electrochemical cell 200 includes a first electrode (e.g., a negative electrode) 202 , a second electrode (e.g., a positive electrode) 204 , a first separator 205 , a second separator 206 , a gate electrode 207 between first electrode 202 and second electrode 204 and between first separator 205 and second separator 206 , an electrolyte 212 , and optionally includes one or more layers (e.g., coatings) 214 , 216 including getter material.
  • Electrochemical cell 200 can optionally include getter material incorporated into one or more of first electrode 202 , second electrode 204 , first separator 205 , second separator 206 and/or electrolyte 212 .
  • Gate electrode 207 is in electrochemical communication with electrolyte 212 and permeable to at least one mobile species that is redox-active to at least one of first electrode 202 and second electrode 204 .
  • at least one gate electrode 207 is situated between the first electrode 202 and second electrode 204 .
  • gate electrode 207 can include a selected one of an electronically conducting material as freestanding form and an electronically conductive film deposited upon an insulating substrate having porosity and tortuosity. Gate electrode 207 can be connected to external circuit through a dedicated tab.
  • Other electrochemical cells with gate electrode 207 are disclosed in U.S. Patent Publication No. 2016/0006081 in the name of Eaglesham et al.
  • the prismatic or pouch cells include an additional tab composed of a metal foil or carbonaceous material of the same kind as current collectors described herein.
  • Tab 306 , 308 and/or additional tab 310 can be affixed to the current collector by laser or ultrasonic welding, adhesive, or mechanical contact, in order to connect the electrodes to the device outside the packaging.
  • a method of forming an electrochemical cell includes forming a structure comprising a first electrode, a second electrode, and a separator there between, wherein the electrochemical structure includes one or more getters as described herein.
  • one or more components e.g., first electrode, second electrode, separator and/or electrolyte
  • getter material can be coated on or layered over one or more of the electrochemical cell components.
  • FIG. 5 illustrates the mass loss associated with gas evolution, and leakage from cells.
  • Data for “A” in FIG. 5 depicts negligible mass loss and corresponds to cells comprising a getter in intimate contact with the electrode assembly and non-aqueous electrolyte.
  • Data for “B” in FIG. 5 is for the same cell construction without the getter, and depicts seven times higher mass loss under the same thermal conditions.
  • a positive electrode was prepared by coating a formulation of lithium cobalt oxide, carbon, and polymeric binder from solution of N-methyl pyrrolidinone upon an aluminum substrate. Subsequently a composite getter comprising LiOH and carbon was spray coated upon the positive electrode from a solution of methanol. The methanol is subsequently removed. Electrochemical cells comprising a positive electrode coated with LiOH and carbon composite getter, a polyolefin separator, and a negative electrode of lithium metal electrochemically plated upon a copper substrate were constructed by stacking. Subsequently the stack was sealed a soft-pouch laminate material after being charged with an electrolyte comprising at least one non-aqueous solvent and salt that does not readily hydrolyze. FIG.

Abstract

An electrochemical cell including a getter material, a battery including the electrochemical cell, and methods of forming the electrochemical cell and battery are disclosed.

Description

    CROSS-REFERENCE TO RELATED APPLICATION
  • The present disclosure claims the benefit of U.S. Provisional Patent Application No. 62/539,393, filed on Jul. 31, 2017 and entitled “ELECTROCHEMICAL CELL WITH GETTER AND METHOD OF FORMING SAME,” which is incorporated herein by reference.
  • FIELD OF INVENTION
  • The disclosure generally relates to electrochemical cells. More particularly, exemplary embodiments of the present disclosure relate to electrochemical cells including a getter.
  • BACKGROUND OF THE DISCLOSURE
  • Electrochemical cells, such as rechargeable or secondary electrochemical cells, can be used to power a variety of devices, such as mobile phones, portable computers, other portable devices, electric or hybrid cars, as well as many other appliances. For many applications, it is desirous to use electrochemical cells with relatively high energy density (energy that can be derived from a cell per unit volume of the cell), relatively high specific energy density (energy that can be derived per unit weight of the cell or per unit weight of the active electrode material), and/or relatively high average discharge potential of the cell, so that desired energy can be supplied to a device using the cell, while minimizing the mass and/or volume of the cell.
  • Generally, electrochemical cells include an anode, a cathode, a separator between the anode and cathode, and an electrolyte. During discharge of an electrochemical cell, an oxidation-reduction reaction occurs, causing electrons flow, through an external circuit, from the anode to the cathode, and cations are attracted from the anode to the cathode. In the case of secondary electrochemical cells, the cells can be recharged by causing electrons and cations to flow in the opposite direction using a charger.
  • During discharging and/or charging of electrochemical cells, particularly of high-energy electrochemical cells (e.g., electrochemical cells with an average discharge potential of 3.5 Volts or more), undesired reactions of one or more components within an electrochemical cell (e.g., between one or more components of the electrolyte and/or between one or more components within an electrolyte and one or more components of an anode and/or a cathode) can occur, resulting in undesired gas production within the cell. For example, one or more of electrolyte components can oxidize or otherwise degrade to form unwanted gas. The produced gas can cause an increase in the cell volume, thereby reducing the energy density of the cell, can cause a reduction of the capacity of the electrochemical cell, can deleteriously affect other discharge performance of the cell, and/or can be a safety hazard.
  • Various attempts to capture gas that is produced in electrochemical cells have been developed. For example, getter material that is sealed apart from the electrochemical cell has been used to capture gas, such as carbon dioxide formed within an electrochemical cell. Unfortunately, placing a seal between the getter material and the electrochemical cell can add undesired weight and/or volume to the electrochemical cell and can prevent the getter material from addressing gas production during regular charging and discharging of the electrochemical cell.
  • U.S. Pat. No. 4,448,860, in the name of von Alpen et al., discloses a cell that is protected against the danger of corrosion of the alkali metal electrode, particularly due to moisture penetrating from the outside the cell, by providing the cell with a gas-absorbing getter material. The gas-absorbing getter material is designed to mitigate danger associated with in-flowing ambient oxygen, CO2, or inwardly diffusing water. The reference does not disclose techniques for addressing gasses that form as a result of high-energy cell operation.
  • U.S. Pat. No. 7,776,465, in the name of Hatazawa et al., discloses a battery that includes an outer covering member that includes a laminated film and battery element (electrochemical cell) contained within the outer covering member and sealed therein. The outer covering member includes a gas absorbable material interposed between the outermost layer of the outer covering member and the battery element. In other words, the gas-absorbable material is not part of the electrochemical cell, but rather is separated from the electrochemical cell and included in an outer covering member.
  • U.S. Pat. No. 8,460,808, in the name of Toia et al., discloses a rechargeable battery that includes means for sorbing harmful substances. The means includes a polymeric housing that is permeable to said harmful substances but impermeable to the electrolyte. One or more getter materials for the sorption of said harmful substances are included within the polymeric housing.
  • U.S. Pat. No. 8,834,180, in the name of Woo et al., discloses a secondary battery that includes an electrode assembly, a gas-collecting member, and a battery case. The electrode assembly includes first and second electrode plates and a separator interposed between the first and second electrode plates. The gas-collecting member is provided separately and adjacent to the electrode assembly. The battery case encases the electrode assembly and the gas-collecting member.
  • U.S. Pat. No. 9,114,382, in the name of Visconti et al., discloses a carbon dioxide composite getter that includes an envelope that is permeable to CO2 and powders of a first and a second active material contained within the envelope. The first active material is lithium hydroxide and the second active material is lithium oxide. The getter is separate from the electrochemical cell, and thus adds significant volume to a battery.
  • Each of the above-described electrochemical cells suffers various drawbacks. Accordingly, improved electrochemical cells including getter material, batteries including the electrochemical cells, and methods of forming the same are desired.
  • SUMMARY OF THE DISCLOSURE
  • Various embodiments of the present disclosure provide improved electrochemical cells including getter material, including one or more gas getters, in direct contact with one or more components of the electrochemical cells—i.e., the getter material or getters are not contained in a separate envelope or container. This allows the getter(s) to work efficiently, without adding significant weight or volume to the cells or batteries including the cells. Use of getters in direct contact with one or more components of the electrochemical cell can also efficiently capture gas that forms within the cell (e.g., within an electrolyte of the cell) during use and/or facilitate high voltage operation of the cells.
  • In accordance with at least one exemplary embodiment of the disclosure, an electrochemical cell, such as a secondary or rechargeable electrochemical cell, includes a first electrode, a second electrode, a separator between the first electrode and the second electrode, a non-aqueous electrolyte, and a getter material comprising one or more gas getters (also referred to herein simply as getter or getters), wherein the one or more gas getters are in direct contact with, form part of, or both one or more of the first electrode, the second electrode, the separator, and the non-aqueous electrolyte. In accordance with various aspects of these embodiments, the non-aqueous electrolyte comprises a salt that does not readily hydrolyze. In accordance with some aspects of these embodiments, the one or more salts do not comprise an anion selected from the group consisting of PF6 −1, BF4 −1, AlCl4 −1, AsF6 −1, ClO4 −1, SiF6 −1, or SbF6 −1. Exemplary salts suitable for use in exemplary electrolytes comprise at least three elements and include two or more of the following: boron, phosphorous, fluorine, carbon, nitrogen, sulfur, and oxygen. Non-limiting examples of exemplary salts of the disclosure include use of one or more salts comprise one or more anions selected from the group consisting of triflate (CF3SO3 −1), triflinate (CF3SO2 −1), perfluorobutanesulfonate (C4F9SO3 −1), bis(perfluoroalkylsulfonyl)imide [N((CxF2x+1)xSO2)2 −1], bis(trifluoromethane) sulfonimide [N(CF3SO2)2 −1], bis(perfluoroethylsulfonyl)imide [N(C2F5SO2)2 −1], bis(fluorosulfonyl)imide [N(SO2F)2 −1], bis(perfluoropinacolato)borate [B(C6F12O2)2 −1], bis(oxalato)borate [B(C2O4)2 −1], difluoro (oxalato) borate [BF2(C2O4)−1], difluoro(malonato) borate [BF2(C3H2O4)−1], bis(benzenesulfonyl)imide [N(C6H5SO2)2 −1], and bis(salicylato)borate [B(C7H4O3)2 −1]. The one or more salts include a cation, such as lithium. In accordance with further aspects, the electrochemical cell is a high-energy rechargeable electrochemical cell with having an average discharge potential of ≥3.5 V, ≥4 V, ≥4.25 V, or ≥4.5 V. In accordance with further aspects, the electrochemical cell is a high-energy rechargeable electrochemical cell having an upper charge cutoff potential of ≥4.3 V, ≥4.35 V, ≥4.4 V, or ≥4.45 V. The electrolyte can be a fluid, such as a liquid or a gel, which may also be in contact with solid ion conductors at least incorporated into the cell electrolyte in part (e.g., polymer, glass, ceramic). The first electrode can include Li, Li alloys such as Si, Sn, Bi, Al, Li4Ti5O12, hard carbon, graphitic carbon, and amorphous carbon. The second electrode can include second electrode active material, such as transition metal oxides, transition metal oxo-anions, chalcogenides, halogenides and combinations thereof. Non-limiting examples of transition metal oxides comprised of one or more transition metals and one or more redox active transition metals such as Lithium Cobalt Oxide, Lithium Nickel Manganese Cobalt Oxide, and Lithium Nickel Cobalt Aluminum Oxide compositions. Non-limiting examples of positive electrode active materials for the Li battery include Lithium metal phosphates and tavorites such as LiFePO4, Lithium metal oxide spinels LiMn2O4, and Li NASICON's Li3V2(PO4)3. The separator can include, for example, porous polypropylene, porous polyethylene, aramid fiber, or glass fiber. The one or more gas getters can include at least one of a metal oxide and a metal hydroxide, such as one or more compounds selected from the group consisting of: LiOH, Li2O, NaOH, Na2O, KOH, K2O, Mg(OH)2, MgO, Ca(OH)2, and CaO in any combination. The getter material can further include one or more of carbon, polymer, resin, metal, or ceramic in any combination. In accordance with exemplary aspects, the getter material does not include any of a silica gel, an alumina, or a zeolite. The getter material can be included as part of a coating that is applied to one or more of the first electrode, the second electrode, and the separator. Additionally or alternatively, the getter material can be incorporated into one or more of the first electrode, the second electrode, the separator, and the electrolyte.
  • In accordance with further exemplary embodiments, a composite getter includes one or more gas getters or gas getter materials (e.g., as described herein) dispersed in a non-aqueous fluid. The gas getter(s) and/or getter material(s) can be dispersed in a non-aqueous fluid as a mixture, suspension, or colloid. The non-aqueous fluid can include one or more (e.g., lithium) salts that do not readily hydrolyze or dissolve in the one or more non-aqueous solvents. In accordance with some aspects of these embodiments, the one or more salts do not comprise an anion selected from the group consisting of PF6 −1, BF4 −1, AlCl4 −1, AsF6 −1, ClO4 , SiF6 −1, or SbF6 −1. For example, the one or more salt may not include the one or more salts do not comprise any of LiPF6, LiBF4, LiAlCl4, LiAsF6, LiClO4, LiSiF6, or LiSbF6. In accordance with further aspects, the non-aqueous fluid comprises one or more salts of at least one of the following anions: triflate (CF3SO3 −1), triflinate (CF3SO2 −1), perfluorobutanesulfonate (C4F9SO3 −1), bis(perfluoroalkylsulfonyl)imide [N((CxF2x+1)xSO2)2 −1], bis(trifluoromethane) sulfonimide [N(CF3SO2)2 −1], bis(perfluoroethylsulfonyl)imide [N(C2F5SO2)2 −1], bis(fluorosulfonyl)imide [N(SO2F)2 −1], bis(perfluoropinacolato) borate [B(C6F12O2)2 −1], bis(oxalato)borate [B(C2O4)2 −1], difluoro (oxalato) borate [BF2(C2O4)−1], difluoro(malonato) borate [BF2(C3H2O4)−1], bis(benzenesulfonyl)imide [N(C6H5SO2)2 −1], and bis(salicylato)borate [B(C7H4O3)2 −1]. In accordance with additional exemplary aspects, the one or more salts comprise at least three elements and include two or more of the following: boron, phosphorous, fluorine, carbon, nitrogen, sulfur, and oxygen. The non-aqueous fluid can include at least one solvent that is a non-aqueous polar aprotic solvent. In accordance with further aspects, the non-aqueous fluid comprises at least one solvent including: ethers, organic carbonates, tertiary amines, lactones, ketones, glymes, nitriles, ionic liquids, aliphatic and aromatic hydrocarbon solvents, and organic nitro solvents. By way of examples, the non-aqueous fluid comprises at least one solvent including THF, 2-methyl THF, dimethoxyethane, diglyme, triglyme, tetraglyme, diethoxyethane, diethylether, proglyme, ethyl diglyme, butyl diglyme, fluorinated ether, hydrofluoroethers, ethylene carbonate, fluoro-ethylene carbonate, dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate, dimethylsulfoxide, dimethylsulfite, sulfolane, ethyl methyl sulfone, acetonitrile, hexane, toluene, fluoro-toluene, nitromethane, 1-3 dioxalane, 1-3 dioxane, 1-4 dioxane, trimethyl phosphate, tri-ethyl phosphate, hexa-methyl-phosphoramide (HMPA), N,N-propyl-methyl-pyrrolidinium-bis(trifluoromethylsulfonyl)imide (P13-TFSI), N,N-propyl-methyl-pyrrolidinium-diacetamide (P13-DCA), propyl-methyl-pyrrolidinium-bis(fluorosulfonyl)imide (P13-FSI), ethyl-dimethyl-propyl-ammonium-bis(trifluoromethylsulfonyl)imide (PDEA-TFSI), and 1-(methoxyethyl)-1-methylpiperidinium-bis(trifluoromethylsulfonyl)imide (MOEMPP-TFSI). A concentration of the salt, or a combination of the one or more salts in the non-aqueous fluid ranges from, for example, about 0.01 M to about 10 M. The composite getter can be incorporated into one or more components of an electrochemical device, such as the electrochemical cells, and batteries described herein. For example, the composite getter can be or be incorporated into a coating that is applied to one or more of electrodes, packaging material, and the insulating separator of the electrochemical cell. The electrochemical cell or device can be configured to charge to, for example, greater than or equal to 4.0 V or other voltages described herein.
  • In accordance with further exemplary embodiments of the disclosure, a battery includes one or more electrochemical cells as described herein. The batteries can additionally include a casing and/or one or more leads. Exemplary batteries can be in the form of coin battery, a soft pack cell laminate, a cylindrical cell, or the like.
  • In accordance with additional exemplary embodiments of the disclosure, a method of forming an electrochemical cell includes the steps of forming a structure comprising a first electrode, a second electrode, and a separator between the first and second electrodes, and providing a getter material in direct contact with one or more of the first electrode, the second electrode, and the separator, and the electrolyte. For example, the method can include introducing a mixture, solution, colloid, or suspension of getter material and a liquid to the structure, wherein the getter material directly contacts one or more of the first electrode, the second electrode, and the separator, removing at least a portion of the liquid, and after removing at least a portion of the liquid, adding an electrolyte solution to the structure. A battery can be formed by adding a casing around the electrochemical cell. Non-limiting examples of the liquid employed to introduce the getter material as a mixture, solution, colloid, or suspension include water, alcohol, ester, ketone, ether, lactam, amide, nitrile, methanol, ethanol, isopropanol, carbonate, ethyl methyl carbonate, dimethyl carbonate, tetrahydrofuran, 1, 2-dimethoxy ethane, acetone, N-methyl-2-pyrrolidone, and acetonitrile.
  • Both the foregoing summary and the following detailed description are exemplary and explanatory only and are not restrictive of the disclosure or the claimed invention.
  • BRIEF DESCRIPTION OF THE DRAWING FIGURES
  • A more complete understanding of the embodiments of the present disclosure may be derived by referring to the detailed description and claims when considered in connection with the following illustrative figures.
  • FIG. 1 illustrates an electrochemical cell in accordance with at least one exemplary embodiment of the disclosure.
  • FIG. 2 illustrates another electrochemical cell in accordance with at least one exemplary embodiment of the disclosure.
  • FIG. 3 illustrates a battery in accordance with at least one exemplary embodiment of the disclosure.
  • FIG. 4 illustrates a typical voltage profile for a cell containing a getter in intimate contact with an electrode assembly and a non-aqueous electrolyte (darker line) as compared to the same cell construction without the getter (lighter line).
  • FIG. 5 illustrates the mass loss for a set of 4.5 Ah cells containing a getter in intimate contact with the electrode assembly and non-aqueous electrolyte (A) as compared to the same cell construction without the getter (B).
  • FIG. 6 illustrates the mass loss for 5 Ah cells containing a getter in intimate contact with an electrode assembly and non-aqueous electrolyte (C) as compared to the same cell construction without the getter (D).
  • FIG. 7 illustrates a typical voltage profile for a cell containing a getter coated upon an electrode surface in intimate contact with non-aqueous electrolyte (darker line) as compared to the same cell construction without the getter (lighter line).
  • It will be appreciated that elements in the figures are illustrated for simplicity and clarity and have not necessarily been drawn to scale. For example, the dimensions of some of the elements in the figures may be exaggerated relative to other elements to help to improve understanding of illustrated embodiments of the present disclosure.
  • DETAILED DESCRIPTION OF EXEMPLARY EMBODIMENTS OF THE INVENTION
  • The description of exemplary embodiments of electrochemical cells, batteries, and methods provided below is merely exemplary and is intended for purposes of illustration only; the following description is not intended to limit the scope of the disclosure or the claims. Moreover, recitation of multiple embodiments having stated features is not intended to exclude other embodiments having additional features or other embodiments incorporating different combinations of the stated features.
  • Additionally, in this disclosure, any ranges indicated may include or exclude the endpoints. Any values of variables indicated (regardless of whether they are indicated with “about” or not) may refer to precise values or approximate values and include equivalents, and may refer to average, median, representative, majority, or a single value.
  • As set forth in more detail below, various embodiments of the specification relate to electrochemical cells that include a getter or getter material in direct contact with or that forms part of one or more components of an electrochemical cell that can form part of a battery. Exemplary electrochemical cells described herein maintain a relatively high energy density, specific energy, and/or can operate at relatively high energy levels (e.g., average discharge voltages of ≥3.5 V, ≥4 V, ≥4.25 V, or ≥4.5 V). In accordance with further aspects, the electrochemical cell is a high-energy rechargeable electrochemical cell having an upper charge cutoff potential of ≥4.3 V, ≥4.35 V, ≥4.4 V, or ≥4.45 V. Further, exemplary electrochemical cells are relatively safe, because the getter captures an amount of gas that is produced within a battery and therefore reduces a likelihood of battery rupture. Examples of this disclosure can be used to form a variety of types of electrochemical cells. For illustration purposes, specific embodiments are described herein in the context of rechargeable, or secondary, lithium-based electrochemical cells such as lithium-ion electrochemical cells and rechargeable lithium metal cells, and those that combine attributes of both. However, the disclosure is not limited to such examples, unless otherwise noted.
  • Lithium-ion cells generally contain active materials that operate on the principle of intercalation wherein Li+ ions migrate in and out of host structures (e.g., graphitic negative electrodes and layered transition metal oxide positive electrode materials) without breaking and forming chemical bonds. Hence there is relatively little structural change (e.g., ≤5% volume expansion) within the electrode materials, and therefore the cell. Generally, this provides a high degree of reversibility for the electrochemical reactions in the cell, with minimal reaction surface area; however it also limits the energy density of the electrode, and therefore the cell. It is generally accepted that significant improvement in energy density will employ higher voltage materials (e.g., coated LiCoO2, High Ni “NMC”), or migration away from pure intercalation reaction to those reactions using the breaking and forming of chemical bonds, because the latter reactions allow for denser storage of Li-ions than do intercalation hosts. Among these are conversion, or displacement reactions, alloying reactions, and metal deposition. That said, dense storage of Li-ions coincides with relatively large structural change and surface area exposure (e.g., ≥5% volume expansion) within the electrode materials and therefore the cell. That is, the migration towards higher energy cell chemistry generally follows two paths: higher voltage and higher surface area reactions to allow for denser storage of Li. A high degree of repeated and uncontrolled surface area change and/or high voltage can facilitate a greater degree of parasitic chemical reactions, resulting in deterioration of the cell, cycle life, power density, and margin for safe operation-thus offsetting gains in energy density. Furthermore, such parasitic reactions can results in formation of gaseous products due to parasitic reactions between electrolyte components and/or between electrolyte components and electrode surfaces. Electrochemical cells including a getter in contact with or that forms part of one or more of the electrochemical cell components can address these issues.
  • FIG. 1 illustrates an electrochemical cell 100 in accordance with exemplary embodiments of the disclosure. Electrochemical cell 100 includes a first electrode 102, a second electrode 104, a separator 106 interposed between first electrode 102 and second electrode 104, a fluid electrolyte 112 in contact with first and second electrodes 102, 104, and optionally includes one or more layers (e.g., coatings) 114, 116, including getter material. As described in more detail below, electrochemical cell 100 can additionally or alternatively include getter material incorporated into one or more of first electrode 102, second electrode 104, separator 106, and/or electrolyte 112. Although electrochemical cell 100 is illustrated with two layers 114, 116 including getter material, as described in more detail below, electrochemical cells in accordance with the disclosure can include additional getter material layers, only one of layers 114, 116, or may not include either of layers 114, 116. In the illustrated example, electrochemical cell 100 also includes a first current collector 108 in electrical contact with first electrode 102 and a second current collector 110 in contact with the second electrode.
  • First electrode 102 (also sometimes referred to herein as a negative electrode or anode) comprises a negative electrode active material that can accept cations. Non-limiting examples of negative electrode active material for lithium-based electrochemical cells include Li, Li alloys such as Si, Sn, Bi, and/or Al alloys, Li4Ti5O12, hard carbon, graphitic carbon, and/or amorphous carbon. Non-limiting examples of negative electrode active material for other rechargeable electrochemical cells include, Mg, Na, Ca, and alloys thereof, hard carbon, graphitic carbon, and/or amorphous carbon. In accordance with some embodiments of the disclosure, most (e.g., greater than 90 wt % to all) of the anode active material can be initially included in a discharged second electrode 104 (also sometimes referred to herein as a positive electrode or cathode) when electrochemical cell 100 is initially made, so that the electrode active material forms part of first electrode 102 during a first charge of electrochemical cell 100—thus providing for a rechargeable electrochemical cell wherein N/P ratio <4. That is, a rechargeable cell wherein the capacity of the first electrode 102, N, and the capacity of the second electrode 104, P, are configured such that N/P is <4. A technique for depositing electroactive material on a portion of first electrode 102 or first current collector 108 using this technique is described in U.S. Patent Publication No. 2016/0172660, in the name of Fischer et al., and similarly in U.S. Patent Publication No. 2016/0172661, in the name of Fischer et al., the contents of which are hereby incorporated herein by reference, to the extent such contents do not conflict with the present disclosure.
  • First electrode 102 and second electrode 104 can further include one or more electronically conductive additives. Non-limiting examples of electronically conductive additives include carbon black, Super P®, C-NERGY™ Super C65, Ensaco® black, Ketjenblack®, acetylene black, synthetic graphite such as Timrex® SFG-6, Timrex® SFG-15, Timrex® SFG-44, Timrex® KS-6, Timrex® KS-15, Timrex® KS-44, natural flake graphite, carbon nanotubes, fullerenes, hard carbon, or mesocarbon microbeads. First electrode 102 can include any combination of the one or more electronically conductive additives.
  • In accordance with some embodiments of the disclosure, first electrode 102 and/or second electrode 104 further includes one or more polymer binders. Non-limiting examples of polymer binders include poly-vinylidene fluoride (PVdF), poly(vinylidene fluoride-co-hexafluoropropene) (PVdF-HFP), Polytetrafluoroethylene (PTFE), Kynar Flex® 2801, Kynar® Powerflex LBG, and Kynar® HSV 900, and Teflon®. First electrode 102 and/or second electrode 104 can include any combination of the one or more polymer binders.
  • In accordance with further exemplary embodiments, first electrode 102 is configured to provide >1000 mAh/cc. Non-limiting exemplary techniques for forming such electrodes are described in U.S. Patent Publication No. 2016/0172661.
  • First electrode 102 can optionally include getter material, which includes one or more gas getters. The one or more gas getters can comprise one or more compounds selected from the group consisting of metal oxides and metal hydroxides. In these cases, a molar ratio of the metal oxides:metal hydroxides can depend on desired characteristics of the getters. For example, the getter material can include more metal hydroxide(s) to increase a speed of gas absorption or more metal oxide(s) to increase a capacity to capture gas. Exemplary getters include compounds selected from the group consisting of: LiOH, Li2O, NaOH, Na2O, KOH, K2O, Mg(OH)2, MgO, Ca(OH)2, and CaO, which can be combined in any combination, or be one compound from the group. Exemplary molar ratios of metal oxide(s) to metal hydroxide(s) range from about 0 to about 1, about 0.5 to about 0.5, or about 1 to about 0.
  • In addition to one or more getters, getter material can include one or more of carbon, polymer, resin, metal, or ceramic, in any combination. Such additional material(s) can be used to, for example, facilitate incorporation of the getter into one or more components of an electrochemical cell (e.g., electrode, separator, or electrolyte) or coat getter material onto the one or more of the components. In accordance with further exemplary embodiments of this disclosure, getter material does not comprise any of a silica gel, an alumina, or a zeolite. An amount of the one or more gas getter can be a molar ratio equivalent (about more—e.g., about two, five, or ten percent more) to the mols of gas (e.g., CO2, CO, H2S, NO2, SO2, H2O, H2, O2, C2H4, C3H6, CxH4*x, hydrocarbons) expected to be produced during charging and/or discharging of electrochemical cell 100.
  • Second electrode 104 (as noted above, also sometimes referred to herein as a positive electrode or cathode) can include intercalation material. Exemplary intercalation materials include transition metal oxides, transition metal oxo-anions, chalcogenides, halogenides and combinations thereof. Non-limiting examples of positive electrode active materials for the lithium electrochemical cells include lithium transition metal oxides comprised of one or more transition metals and one or more redox active transition metals such as lithium cobalt oxide, lithium nickel manganese cobalt oxide compositions, lithium nickel cobalt aluminum compositions, and lithium metal phosphates and tavorites such as LiFePO4, lithium metal oxide spinels LiMn2O4, and Li NASICON's Li3V2(PO4)3. By way of examples lithium nickel manganese cobalt oxide “NMC” can include a variety of transition metal ratios and lithium excess. Exemplary NMC ratios include, but are not limited to, Li[Ni1/3Mn1/3Co1/3]O2 or so-called “111”, Li[Ni5/3Mn3/3Co2/3]O2 or so-called “532”, Li[Ni6/3Mn2/3Co2/3]O2 or so-called “622”, Li[Ni8/3Mn1/3Co1/3]O2 or so-called “811” either with stoichiometric or excess lithium to transition metals. In addition, second electrode 104 may comprise conversion, or displacement, reaction materials. Non-limiting examples of conversion, or displacement reaction materials includes sulfur, metal nitrides, metal phosphides, metal sulfides, metal oxides, metal fluorides, metal chlorides such as FeF3, FeF2, NiF2, CO3O4, ZnF2, FeS2, Li2O and at least one metal, LiF and at least one metal, In addition, second electrode 104 may comprise an organic, or polymeric electro-active material. Non-limiting examples include quinones such as dimethoxy benzoquinone, poly-anthraquinone, graphene, graphene oxide. As noted above, second electrode 104 can initially include most or all of the active material for first electrode 102. Similar to first electrode 102, second electrode 104 can optionally include getter material as described herein.
  • In accordance with exemplary embodiments of the disclosure, at least one of the first electrode 102 and the second electrode 104 include a metal, an alloy, or an intermetallic compound. In accordance with additional or alternative exemplary embodiments, at least one of the first electrode 102 and the second electrode 104 include a material configured to undergo an insertion reaction, an alloying, an intercalation, a disproportionation, a conversion reaction, or any combination thereof.
  • Separator 106 electrically isolates the first electrode from the second electrode and is permeable to at least one mobile species which is redox-active at least one of the first electrode and the second electrode. Exemplary materials suitable for separator 106 in accordance with embodiments of the disclosure include porous virgin or coated polyolefin, polypropylene, polyethylene, aramix fiber, and glass fiber. Separator 106 can optionally comprise the getter material in part or entirely as described herein.
  • Electrolyte 112 can be a fluid, e.g., a liquid or a gel electrolyte, which may also be in contact with solid ion conductors at least incorporated into the cell electrolyte in part (e.g., polymer, glass, ceramic). Electrolyte 112 generally includes a solvent and one or more salts. Electrolyte 112 can, in some cases, also include getter material as described herein.
  • A variety of non-aqueous (e.g., organic) solvents are suitable for use in the electrolyte 112. Non-aqueous solvents can be used alone or in any suitable combination. Whether a solvent comprises a single non-aqueous composition or a plurality of non-aqueous compositions, for the purposes of further exposition, the non-aqueous solvent will be referred to as “the solvent” in the singular. In order to provide for the reversible dissolution and plating of an electroactive metal, the solvent advantageously should provide appreciable solubility by coordination of the constituent inorganic salts of the electroactive metal. In accordance various examples, suitable solvents include non-aqueous polar aprotic solvents, ethers, organic carbonates, and tertiary amines, and may also include, lactones, ketones, glymes, nitriles, ionic liquids, aliphatic and aromatic hydrocarbon solvents and organic nitro solvents. More specifically, suitable solvents include THF, 2-methyl THF, dimethoxyethane, diglyme, triglyme, tetraglyme, diethoxyethane, diethylether, proglyme, ethyl diglyme, butyl diglyme, fluorinated ether, hydrofluoroethers, ethylene carbonate, fluoro-ethylene carbonate, dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate, dimethylsulfoxide, dimethylsulfite, sulfolane, ethyl methyl sulfone, acetonitrile, hexane, toluene, fluoro-toluene, nitromethane, 1-3 dioxalane, 1-3 dioxane, 1-4 dioxane, trimethyl phosphate, tri-ethyl phosphate, hexa-methyl-phosphoramide (HMPA), N,N-propyl-methyl-pyrrolidinium-bis(trifluoromethylsulfonyl)imide (P13-TFSI), N,N-propyl-methyl-pyrrolidinium-diacetamide (P13-DCA), propyl-methyl-pyrrolidinium-bis(fluorosulfonyl)imide (P13-FSI), ethyl-dimethyl-propyl-ammonium-bis(trifluoromethylsulfonyl)imide (PDEA-TFSI), and 1-(methoxyethyl)-1-methylpiperidinium-bis(trifluoromethylsulfonyl)imide (MOEMPP-TFSI).
  • Exemplary salts for electrolyte 112 do not readily hydrolyze. For purposes of this disclosure, salts that do not readily hydrolyze are salts that do not react with trace amounts (e.g., <3000 ppm) water in a autocatalytic decomposition reaction to form significant amounts (e.g., more than 300 ppm) of strong acid such as HF or HCl. In accordance with further exemplary embodiments, the one or more salts do not comprise an anion selected from the group consisting of PF6 −1, BF4 −1, AlCl4 −1, AsF6 −1, ClO4 −1, SiF6 −1, or SbF6 −1. Salts including such anions are thought to be susceptible to hydrolysis. By way of specific examples, the one or more salts do not include any of LiPF6, LiBF4, LiAlCl4, LiAsF6, LiClO4, LiSiF6, or LiSbF6. Exemplary compounds suitable for the one or more salts comprise at least three elements and include two or more of the following: boron, phosphorous, fluorine, carbon, nitrogen, and oxygen. Non-limiting examples of exemplary salts of the disclosure include use of one or more salts comprise one or more anions selected from the group consisting of triflate (CF3SO3 −1), triflinate (CF3SO2 −1), perfluorobutanesulfonate (C4F9SO3 −1), bis(perfluoroalkylsulfonyl)imide [N((CxF2x+1)xSO2)2 −1], bis(trifluoromethane)sulfonimide [N(CF3SO2)2 −1], bis(perfluoroethylsulfonyl)imide [N(C2F5SO2)2 −1], bis(fluorosulfonyl)imide [N(SO2F)2 −1], bis(perfluoropinacolato) borate [B(C6F12O2)2 −1], bis(oxalato)borate [B(C2O4)2 −1], difluoro (oxalato) borate [BF2(C2O4)−1], difluoro(malonato) borate [BF2(C3H2O4)−1], bis(benzenesulfonyl)imide [N(C6H5SO2)2 −1], and bis(salicylato)borate [B(C7H4O3)2 −1]. The cation can be lithium, sodium, magnesium, or calcium. A concentration of the salt, or a combination of salts in the electrolyte solution ranges from about 0.01 M to about 10 M, about 0.1 M to about 7 M, or about 0.25 to about 7 M, or from about 0.5 M to saturation. Without wishing to be bound by theory, it is thought that the use of non-aqueous fluid electrolyte comprising salts that do not readily hydrolyze permits the function of the gas getter material(s), and may in fact even expedite the gettering activity of such materials, while in intimate contact with the non-aqueous fluid electrolyte.
  • First current collector 108 and/or second current collector 110 can include any material capable of sufficiently conducting electrons. Exemplary first/second electrode current collector 108/110 materials include aluminum, aluminum alloys, copper, copper alloys, nickel, nickel alloys, titanium, titanium alloys, steel, carbonaceous materials, and a metal substrate coated with an over-layer to prevent corrosion in the electrolyte.
  • As noted above, electrochemical cell 100 can include one or more layers 114, 116 of getter material. Layers 114 and/or 116 can be initially coated onto one or more surfaces of one or more of first electrode 102, second electrode 104 and/or separator 106. Generally, when electrochemical cell 100 includes layer 114 and/or layer 116, the layer(s) will be between an electrode 102 or 104 (first or second) and separator 106.
  • FIG. 2 illustrates another electrochemical cell 200 in accordance with additional embodiments of the disclosure. Electrochemical cell 200 is similar to electrochemical cell 100, except electrochemical cell 200 includes a gate electrode 207, in addition to the other cell components. When an electrochemical cell includes a gate electrode, a circuit can be configured to measure an operating parameter of the device and to determine when a cell health event occurs and/or respond to the cell health event, as disclosed in U.S. Patent Publication No. 2016/0006081 in the name of Eaglesham et al., the contents of which are incorporated herein by reference, to the extent such contents do not conflict with the present disclosure.
  • In the illustrated example, electrochemical cell 200 includes a first electrode (e.g., a negative electrode) 202, a second electrode (e.g., a positive electrode) 204, a first separator 205, a second separator 206, a gate electrode 207 between first electrode 202 and second electrode 204 and between first separator 205 and second separator 206, an electrolyte 212, and optionally includes one or more layers (e.g., coatings) 214, 216 including getter material. Electrochemical cell 200 can optionally include getter material incorporated into one or more of first electrode 202, second electrode 204, first separator 205, second separator 206 and/or electrolyte 212.
  • First electrode 202, second electrode 204, first separator 205, second separator 206, electrolyte 212, and one or more layers 214, 216 can be the same or similar to the respective components discussed above in connection with FIG. 1.
  • Gate electrode 207 is in electrochemical communication with electrolyte 212 and permeable to at least one mobile species that is redox-active to at least one of first electrode 202 and second electrode 204. In the illustrated example, at least one gate electrode 207 is situated between the first electrode 202 and second electrode 204. By way of examples, gate electrode 207 can include a selected one of an electronically conducting material as freestanding form and an electronically conductive film deposited upon an insulating substrate having porosity and tortuosity. Gate electrode 207 can be connected to external circuit through a dedicated tab. Other electrochemical cells with gate electrode 207 are disclosed in U.S. Patent Publication No. 2016/0006081 in the name of Eaglesham et al.
  • Batteries
  • A battery can include one or more electrochemical cells, such as electrochemical cell 100 or electrochemical cell 200. The battery can be a button or coin cell battery comprising discs of electrochemical cell components (electrode and separator) that sit in a can base onto which a can lid is crimped. In other embodiments, the battery is a stacked cell battery. In other embodiments, the battery is a prismatic or pouch cell comprising one or more stacked electrochemical cells sandwiched between current collectors.
  • FIG. 3 illustrates an exemplary soft pack cell laminate battery 300 that includes an electrochemical cell 302, which can be the same or similar to electrochemical cell 100 or electrochemical cell 200, and first and second tabs 306 and 308. First tab 306 can form contact to a first electrode (e.g., first electrode 102/202); second tab can form contact to a second electrode (e.g., second electrode 104/204). Battery 300 can optionally include one or more third tabs 310 that are electrically coupled to a gate electrode, if present. Electrochemical cell 302 can include a folded electrochemical cell (e.g., cell 100/200), which can be within a (e.g., polymer coated aluminum foil) pouch 304. Pouch 304 can be vacuum and heat dried, filled with electrolyte (e.g., electrolyte 112, 212), and vacuum and heat sealed. In other embodiments, the battery is a prismatic or pouch bi-cell comprising one or more stacks of a positive electrode that is coated with active material on both sides and wrapped in porous separator, and a negative electrode folded around the positive electrode, wherein one or both current collectors can comprise carbonaceous materials. These electrochemical cells can be folded within a (e.g., polymer coated aluminum foil) pouch, dried under heat and/or vacuum, filled with electrolyte, and vacuum and heat sealed. Getter material can be added to the battery as described below. In accordance with some embodiments, the prismatic or pouch cells include an additional tab composed of a metal foil or carbonaceous material of the same kind as current collectors described herein. Tab 306, 308 and/or additional tab 310 can be affixed to the current collector by laser or ultrasonic welding, adhesive, or mechanical contact, in order to connect the electrodes to the device outside the packaging.
  • In accordance with yet additional embodiments, the battery is a wound or cylindrical cell comprising one or more electrochemical cells as described herein. In this case, the battery can include wound layers of one or more stacks of a positive electrode which comprises active material coated upon an electronically conducting substrate, sandwiched between layers of porous separator, and a negative electrode comprising active material coated upon an electronically conducting substrate. The stack(s) can be wound into cylindrical roll, inserted into the can, dried under heat and/or vacuum, filled with electrolyte, and vacuum and welded shut. Getter material can be added to the battery as described below. In some embodiments of the cylindrical cells described herein, an additional tab composed of a metal foil or conducting material of the same kind as current collectors described herein, is affixed to the current collector by laser or ultrasonic welding, adhesive, or mechanical contact, in order to connect the electrodes to an external circuit outside the packaging.
  • In accordance with additional embodiments of the disclosure, a method of forming an electrochemical cell includes forming a structure comprising a first electrode, a second electrode, and a separator there between, wherein the electrochemical structure includes one or more getters as described herein. As noted above, one or more components (e.g., first electrode, second electrode, separator and/or electrolyte) can include getter material and/or getter material can be coated on or layered over one or more of the electrochemical cell components.
  • In accordance with some embodiments of the disclosure, a method of forming an electrochemical cell includes providing a mixture of getter material and a liquid (e.g., water, alcohol, ester, ketone, ether, lactam, amide, nitrile, methanol, ethanol, isopropanol, carbonate, ethyl methyl carbonate, dimethyl carbonate, tetrahydrofuran, 1, 2-dimethoxy ethane, acetone, N-methyl-2-pyrrolidone, and acetonitrile) employed to introduce the getter material as a mixture, solution, or suspension to the structure, wherein the getter material directly contacts one or more of the first electrode, the second electrode, and the separator, removing at least a portion of the liquid, and after removing at least a portion of the liquid, adding an electrolyte solution to the structure. A battery can be formed by forming and/or sealing a casing around the electrochemical cell.
  • EXAMPLES
  • The following non-limiting examples illustrate comparative electrochemical cells and electrochemical cells in accordance with exemplary embodiments of the disclosure. These examples are merely illustrative, and it is not intended that the invention be limited to the examples.
  • In the following examples and the comparative example, lithium-ion electrochemical cells were prepared by the following steps:
  • Example 1
  • Electrochemical cells comprising a lithium cobalt oxide “LCO” positive electrode, a polyolefin separator, and a negative electrode of lithium metal electrochemically plated upon a copper substrate were constructed by winding the three components in a manner to form a flat wound, prismatic stack with a nominal capacity of about 5.0 Ah. Subsequently the stack was sealed a soft-pouch laminate material after being charged with an electrolyte comprising at least in part ethylene carbonate, dimethyl carbonate, and lithium difluoro(oxalato)borate, a salt that does not readily hydrolyze. One cell includes a getter comprising a mixture of Li2O and LiOH deposited in intimate contact with the electrode assembly and electrolyte. FIG. 4 illustrates a typical voltage profile for a cell containing a getter in intimate contact with an electrode assembly and a non-aqueous electrolyte (darker line) as compared to the same cell construction without the getter (lighter line). The cells depicted are first charged at a rate of 0.2 C to greater than 4.25 V, then discharged at a rate of 0.2 C. Subsequently they are re-charged at a higher rate of 0.33 C to greater than 4.25 V. It is apparent by way of comparing the shape of the voltage profile and corresponding capacity that there is no additional electrochemical activity due to the presence of the getter in intimate contact with the electrode assembly and electrolyte.
  • Example 2
  • A series of cells were constructed in similar fashion as described in Example 1 presented herein. The cells, some comprising getter and some excluding getter, are charged to greater than 4.25 V and 4.5 Ah, then subjected to ambient humidity and a temperature of nearly 80° C. for greater than 50 hours. FIG. 5 illustrates the mass loss associated with gas evolution, and leakage from cells. Data for “A” in FIG. 5 depicts negligible mass loss and corresponds to cells comprising a getter in intimate contact with the electrode assembly and non-aqueous electrolyte. Data for “B” in FIG. 5 is for the same cell construction without the getter, and depicts seven times higher mass loss under the same thermal conditions.
  • Example 3
  • A series of cells were constructed in similar fashion, but with a lithium nickel manganese oxide cathode as described in Example 1 presented herein. The cells, some comprising getter and some excluding getter, are charged to greater than 4.25 V and 5.0 Ah, then subjected to ambient humidity and a temperature of nearly 80° C. for different periods of time. FIG. 6 illustrates the mass loss associated with gas evolution, and leakage from cells. Data for “C” in FIG. 6 depicts negligible mass loss after 60 hours at temperature of nearly 80° C. and corresponds to cells comprising a getter comprising a 3:1 mixture of LiOH and Li2O in intimate contact with the electrode assembly and non-aqueous electrolyte. Data for “D” in FIG. 6 is for the same cell construction without the getter, and depicts a few percent mass loss due to a high rate of gas evolution and leakage after only 18 hours at temperature of nearly 80° C.
  • Example 4
  • A positive electrode was prepared by coating a formulation of lithium cobalt oxide, carbon, and polymeric binder from solution of N-methyl pyrrolidinone upon an aluminum substrate. Subsequently a composite getter comprising LiOH and carbon was spray coated upon the positive electrode from a solution of methanol. The methanol is subsequently removed. Electrochemical cells comprising a positive electrode coated with LiOH and carbon composite getter, a polyolefin separator, and a negative electrode of lithium metal electrochemically plated upon a copper substrate were constructed by stacking. Subsequently the stack was sealed a soft-pouch laminate material after being charged with an electrolyte comprising at least one non-aqueous solvent and salt that does not readily hydrolyze. FIG. 7 illustrates a typical voltage profile for a cell comprising a getter in intimate contact with an electrode assembly (i.e., coated upon the positive electrode and therefore situated in the stack between the positive electrode and separator) and a non-aqueous electrolyte (darker line) as compared to the same positive electrode without the getter coating in the cell construction (lighter line). The cells depicted are charged at a rate of 1C to greater than 4.25 V, then discharged at a rate of 1C in this cycling scheme. It is apparent by way of comparing the shape of the voltage profile and corresponding capacity that there is no deleterious electrochemical activity due to the presence of the getter in intimate contact with the electrode assembly and electrolyte.
  • Although exemplary embodiments of the present disclosure are set forth herein, it should be appreciated that the disclosure is not so limited. For example, although the systems and methods are described in connection with various specific chemistries, the disclosure is not necessarily limited to these chemistries. Various modifications, variations, and enhancements of the systems and methods set forth herein can be made without departing from the spirit and scope of the present disclosure.

Claims (20)

What is claimed is:
1. An electrochemical cell comprising:
a first electrode;
a second electrode;
a separator between the first electrode and the second electrode;
a non-aqueous electrolyte comprising one or more salts; and
a getter material comprising one or more gas getters,
wherein the one or more gas getters are in direct contact with, form part of, or both one or more of the first electrode, the second electrode, the separator, and the non-aqueous electrolyte.
2. The electrochemical cell of claim 1, wherein the one or more salts do not readily hydrolyze.
3. The electrochemical cell of claim 1, wherein the non-aqueous electrolyte comprises a fluid.
4. The electrochemical cell of claim 1, wherein the one or more gas getters comprise at least one of a metal oxide, a metal hydroxide, or both the metal oxide and the metal hydroxide.
5. The electrochemical cell of claim 2, wherein the one or more salts do not comprise an anion selected from the group consisting of PF6 −1, BF4 −1, AlCl4 −1, AsF6 −1, ClO4 −1, SiF6 −1, or SbF6 −1.
6. The electrochemical cell of claim 2 wherein the one or more salts do not comprise any of LiPF6, LiBF4, LiAlCl4, LiAsF6, LiClO4, LiSiF6, or LiSbF6.
7. The electrochemical cell of claim 1, wherein the non-aqueous electrolyte comprises one or more lithium salts of at least one of the following anions: triflate (CF3SO3 −1), triflinate (CF3SO2 −1), perfluorobutanesulfonate (C4F9SO3 −1), bis(perfluoroalkylsulfonyl)imide [N((CxF2x+1)xSO2)2 −1], bis(trifluoromethane)sulfonimide [N(CF3SO2)2 −1], bis(perfluoroethylsulfonyl)imide [N(C2F5SO2)2 −1], bis(fluorosulfonyl)imide [N(SO2F)2 −1], bis(perfluoropinacolato)borate [B(C6F12O2)2 −1], bis(oxalato)borate [B(C2O4)2 −1], difluoro(oxalato)borate [BF2(C2O4)−1], difluoro(malonato)borate [BF2(C3H2O4)−1], bis(benzenesulfonyl)imide [N(C6H5SO2)2 −1], and bis(salicylato)borate [B(C7H4O3)2 −1].
8. The electrochemical cell of claim 1, wherein the getter material is incorporated into a coating that is applied to one or more of the first electrode, the second electrode, and the separator.
9. The electrochemical cell of claim 1, wherein the one or more salts comprise at least three elements and include two or more of the following: boron, phosphorous, fluorine, carbon, nitrogen, sulfur, and oxygen.
10. The electrochemical cell of claim 1, wherein the one or more gas getters comprise one or more compounds selected from the group consisting of: LiOH, Li2O, NaOH, Na2O, KOH, K2O, Mg(OH)2, MgO, Ca(OH)2, and CaO, in any combination.
11. The electrochemical cell of claim 1, wherein a concentration of the salt, or a combination of the one or more salts in the non-aqueous electrolyte ranges from about 0.01 M to about 10 M.
12. The electrochemical cell of claim 1, wherein the getter material comprises one or more of carbon, polymer, resin, metal, or ceramic.
13. The electrochemical cell of claim 12, wherein the getter material does not comprise any of a silica gel, an alumina, or a zeolite.
14. The electrochemical cell of claim 1, wherein the electrochemical cell is configured to charge to greater than or equal to 4.0 V.
15. The electrochemical cell of claim 1, wherein at least one of the first electrode and the second electrode comprises a metal, an alloy, or an intermetallic compound configured to provide >1000 mAh/cc.
16. The electrochemical cell of claim 1, wherein at least one of the first electrode and the second electrode comprises a material configured to undergo an insertion reaction, an alloying, an intercalation, a disproportionation, a conversion reaction, or any combination thereof.
17. A battery comprising one or more electrochemical cells of claim 1.
18. A method of forming an electrochemical cell, the method comprising the steps of:
forming a structure comprising a first electrode, a second electrode, and a separator there between;
providing a mixture of getter material and a liquid to the structure, wherein the getter material directly contacts one or more of the first electrode, the second electrode, and the separator;
removing at least a portion of the liquid; and
after removing at least a portion of the liquid, adding an electrolyte solution to the structure.
19. The method of claim 18, wherein the electrolyte solution comprises at least one of the following anions triflate (CF3SO3 −1), triflinate (CF3SO2 −1), perfluorobutanesulfonate (C4F9SO3 −1), bis(perfluoroalkylsulfonyl)imide [N((CxF2x+1)xSO2)2 −1], bis(trifluoromethane)sulfonimide [N(CF3SO2)2 −1], bis(perfluoroethylsulfonyl)imide [N(C2F5SO2)2 −1], bis(fluorosulfonyl)imide [N(SO2F)2 −1], bis(perfluoropinacolato)borate [B(C6F12O2)2 −1], bis(oxalato)borate [B(C2O4)2 −1], difluoro(oxalato)borate [BF2(C2O4)−1], difluoro (malonato)borate [BF2(C3H2O4)−1], bis(benzenesulfonyl)imide [N(C6H5SO2)2 −1], and bis(salicylato)borate [B(C7H4O3)2 −1].
20. The method of claim 18, wherein the getter material comprises one or more compounds selected from the group consisting of: LiOH, Li2O, NaOH, Na2O, KOH, K2O, Mg(OH)2, MgO, Ca(OH)2, and CaO.
US16/049,535 2017-07-31 2018-07-30 Electrochemical cell with getter and method of forming same Abandoned US20190036179A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US16/049,535 US20190036179A1 (en) 2017-07-31 2018-07-30 Electrochemical cell with getter and method of forming same
US17/200,041 US20210218080A1 (en) 2017-07-31 2021-03-12 Electrochemical Cell With Getter And Method of Forming Same

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US201762539393P 2017-07-31 2017-07-31
US16/049,535 US20190036179A1 (en) 2017-07-31 2018-07-30 Electrochemical cell with getter and method of forming same

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US17/200,041 Continuation US20210218080A1 (en) 2017-07-31 2021-03-12 Electrochemical Cell With Getter And Method of Forming Same

Publications (1)

Publication Number Publication Date
US20190036179A1 true US20190036179A1 (en) 2019-01-31

Family

ID=65038233

Family Applications (3)

Application Number Title Priority Date Filing Date
US16/049,535 Abandoned US20190036179A1 (en) 2017-07-31 2018-07-30 Electrochemical cell with getter and method of forming same
US16/049,550 Active US11081737B2 (en) 2017-07-31 2018-07-30 Getter for use with electrochemical cells, devices including the getter, and method of forming same
US17/200,041 Abandoned US20210218080A1 (en) 2017-07-31 2021-03-12 Electrochemical Cell With Getter And Method of Forming Same

Family Applications After (2)

Application Number Title Priority Date Filing Date
US16/049,550 Active US11081737B2 (en) 2017-07-31 2018-07-30 Getter for use with electrochemical cells, devices including the getter, and method of forming same
US17/200,041 Abandoned US20210218080A1 (en) 2017-07-31 2021-03-12 Electrochemical Cell With Getter And Method of Forming Same

Country Status (3)

Country Link
US (3) US20190036179A1 (en)
CN (1) CN110959220A (en)
WO (1) WO2019027925A1 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10727473B2 (en) 2014-12-12 2020-07-28 Viking Power Systems Pte. Ltd. Electrochemical cell and method of making the same
US10734683B2 (en) 2016-08-12 2020-08-04 Viking Power Systems Pte. Ltd. Additive containing electrolytes for high energy rechargeable metal anode batteries
WO2021104059A1 (en) * 2019-11-26 2021-06-03 深圳先进技术研究院 New type of battery and method for fabrication thereof
US11063297B2 (en) 2017-12-21 2021-07-13 Viking Power Systems Pte, Ltd. Electrochemical cell and electrolyte for same
US11081737B2 (en) 2017-07-31 2021-08-03 Viking Power Systems Pte, Ltd. Getter for use with electrochemical cells, devices including the getter, and method of forming same
US11196088B2 (en) 2019-04-11 2021-12-07 Ses Holdings Pte. Ltd. Localized high-salt-concentration electrolytes containing longer-sidechain glyme-based solvents and fluorinated diluents, and uses thereof

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102019212014A1 (en) * 2019-08-09 2021-02-11 Volkswagen Ag Process for the production of a layer system of a battery cell
EP4195379A1 (en) * 2021-02-25 2023-06-14 LG Energy Solution, Ltd. Battery cell, manufacturing method therefor, and battery module comprising same
CN116368674A (en) * 2021-07-06 2023-06-30 株式会社Lg新能源 Battery cell and battery cell manufacturing apparatus for manufacturing the same
CN215896624U (en) * 2021-08-19 2022-02-22 宁德时代新能源科技股份有限公司 Electrode assembly, battery monomer, battery and consumer
CN113764643A (en) * 2021-09-10 2021-12-07 珠海冠宇动力电池有限公司 Electrode plate and lithium ion battery
CN113991201B (en) * 2021-10-27 2024-01-30 远景动力技术(江苏)有限公司 Gas adsorption diaphragm, preparation method thereof and lithium ion battery

Family Cites Families (38)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3136578A1 (en) 1981-09-15 1983-03-31 Varta Batterie Ag, 3000 Hannover GALVANIC ELEMENT WITH INTEGRATED GETTER
US4541984A (en) * 1982-09-29 1985-09-17 Combustion Engineering, Inc. Getter-lubricant coating for nuclear fuel elements
KR100274884B1 (en) 1998-01-22 2000-12-15 김순택 Prismatic secondary battery righting n/p rate
US6402795B1 (en) 1998-02-18 2002-06-11 Polyplus Battery Company, Inc. Plating metal negative electrodes under protective coatings
DE19827630A1 (en) * 1998-06-20 2000-04-27 Merck Patent Gmbh Purification of battery electrolytes using chemical adsorption
US6168884B1 (en) 1999-04-02 2001-01-02 Lockheed Martin Energy Research Corporation Battery with an in-situ activation plated lithium anode
JP4529207B2 (en) 1999-11-30 2010-08-25 ソニー株式会社 Non-aqueous electrolyte battery
US6706447B2 (en) 2000-12-22 2004-03-16 Fmc Corporation, Lithium Division Lithium metal dispersion in secondary battery anodes
US7041412B2 (en) * 2001-07-23 2006-05-09 Matsushita Electric Industrial Co., Ltd. Non-aqueous electrolyte secondary battery
CN100474688C (en) 2004-05-28 2009-04-01 宇部兴产株式会社 Nonaqueous electrolytic solution and lithium secondary battery
JP4198658B2 (en) 2004-09-24 2008-12-17 株式会社東芝 Nonaqueous electrolyte secondary battery
US7927742B2 (en) 2004-10-29 2011-04-19 Medtronic, Inc. Negative-limited lithium-ion battery
US20060222945A1 (en) * 2005-04-01 2006-10-05 Bowden William L Battery cathodes
ITMI20050904A1 (en) * 2005-05-17 2006-11-18 Getters Spa ADDITIVE FOR ELECTROLYTIC CONDENSERS
US8168330B2 (en) * 2006-04-11 2012-05-01 Enerdel, Inc. Lithium titanate cell with reduced gassing
JP2008146963A (en) * 2006-12-08 2008-06-26 Sony Corp Separator for nonaqueous electrolyte secondary battery, nonaqueous electrolyte secondary battery, and battery pack
ITMI20071147A1 (en) * 2007-06-05 2008-12-06 Getters Spa RECHARGEABLE LITHIUM BATTERIES INCLUDING VEHICLES FOR THE ABSORPTION OF HARMFUL SUBSTANCES
US8715865B2 (en) 2007-07-11 2014-05-06 Basf Corporation Non-aqueous electrolytic solutions and electrochemical cells comprising the same
US20110171534A1 (en) * 2010-01-14 2011-07-14 Ernest Paul Lampert Long lasting high current density charging & discharging, temperature-resistant batteries and related methods
JP2011171096A (en) 2010-02-18 2011-09-01 Sony Corp Nonaqueous electrolyte battery
WO2011135818A1 (en) * 2010-04-28 2011-11-03 パナソニック株式会社 Secondary battery
WO2012029669A1 (en) * 2010-09-02 2012-03-08 株式会社Gsユアサ Battery and battery system
US9227950B2 (en) 2010-10-22 2016-01-05 Mitsui Chemicals, Inc. Cyclic sulfate compound, non-aqueous electrolyte solution containing same, and lithium secondary battery
US8912705B2 (en) * 2011-08-30 2014-12-16 Siemens Industry, Inc. Method and apparatus for insulating induction machine coil connectors
JP5974735B2 (en) 2011-09-05 2016-08-23 ソニー株式会社 Non-aqueous electrolyte for secondary battery, secondary battery, battery pack, electric vehicle, power storage system, electric tool and electronic device
KR101741030B1 (en) 2012-03-08 2017-05-29 삼성에스디아이 주식회사 Secondary battery
ITMI20121207A1 (en) 2012-07-11 2014-01-12 Getters Spa GETTER COMPOSITE FOR CARBON DIOXIDE
JP6303412B2 (en) * 2013-03-19 2018-04-04 株式会社村田製作所 Batteries, electrolyte layers, battery packs, electronic devices, electric vehicles, power storage devices, and power systems
WO2015033619A1 (en) 2013-09-05 2015-03-12 石原産業株式会社 Nonaqueous-electrolyte secondary battery and manufacturing method therefor
WO2015160334A1 (en) 2014-04-15 2015-10-22 Uchicago Argonne, Llc Lithium-sulfur batteries
CN103887473A (en) * 2014-04-20 2014-06-25 天津市捷威动力工业有限公司 Negative electrode with surface coated with lithiated zeolite and lithium ion battery using negative electrode
US10236493B2 (en) 2014-07-02 2019-03-19 Pellion Technologies, Inc. Multi-electrode electrochemical cell and method of making the same
US10367189B2 (en) 2014-09-10 2019-07-30 Battelle Memorial Institute Anode-free rechargeable battery
US10333173B2 (en) * 2014-11-14 2019-06-25 Medtronic, Inc. Composite separator and electrolyte for solid state batteries
KR102588454B1 (en) 2014-12-12 2023-10-11 바이킹 파워 시스템즈 피티이. 엘티디. Electrochemical cell and method of making the same
KR102407139B1 (en) 2015-05-20 2022-06-10 삼성전자주식회사 Lithium metal battery
KR101956334B1 (en) * 2016-01-06 2019-03-08 주식회사 엘지화학 Secondary Battery Having Gas-Adsorbing Polymer
CN110959220A (en) 2017-07-31 2020-04-03 维金电力系统有限公司 Electrochemical cell with getter and method of forming the same

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10727473B2 (en) 2014-12-12 2020-07-28 Viking Power Systems Pte. Ltd. Electrochemical cell and method of making the same
US10734683B2 (en) 2016-08-12 2020-08-04 Viking Power Systems Pte. Ltd. Additive containing electrolytes for high energy rechargeable metal anode batteries
US11081737B2 (en) 2017-07-31 2021-08-03 Viking Power Systems Pte, Ltd. Getter for use with electrochemical cells, devices including the getter, and method of forming same
US11063297B2 (en) 2017-12-21 2021-07-13 Viking Power Systems Pte, Ltd. Electrochemical cell and electrolyte for same
US11196088B2 (en) 2019-04-11 2021-12-07 Ses Holdings Pte. Ltd. Localized high-salt-concentration electrolytes containing longer-sidechain glyme-based solvents and fluorinated diluents, and uses thereof
WO2021104059A1 (en) * 2019-11-26 2021-06-03 深圳先进技术研究院 New type of battery and method for fabrication thereof

Also Published As

Publication number Publication date
US20210218080A1 (en) 2021-07-15
US20190036180A1 (en) 2019-01-31
CN110959220A (en) 2020-04-03
US11081737B2 (en) 2021-08-03
WO2019027925A1 (en) 2019-02-07

Similar Documents

Publication Publication Date Title
US20210218080A1 (en) Electrochemical Cell With Getter And Method of Forming Same
JP4363436B2 (en) Secondary battery
US11430994B2 (en) Protective coatings for lithium metal electrodes
WO2012056765A1 (en) Secondary battery and method for manufacturing same
CN102163710B (en) For the negative pole of lithium rechargeable battery, lithium rechargeable battery, electric tool, motor vehicle and power storage system
US11114696B2 (en) Electrolyte system for lithium-chalcogen batteries
US8999009B2 (en) Surface modification of battery materials and method for making a battery
US20190288273A1 (en) Electrolyte systems for silicon-containing electrodes
US20050238956A1 (en) Negative electrode for lithium battery and lithium battery comprising same
JP6738721B2 (en) Non-aqueous electrolyte solution for secondary battery and non-aqueous electrolyte secondary battery using the same
CN112448047B (en) Method for prelithiation of electrodes
JP2017507460A (en) Multivalent metal salts for lithium ion batteries having oxygen-containing electrode active materials
EP2161776B1 (en) Polyvinylpyridine additives for nonaqueous electrolytes
KR102103378B1 (en) Battery Cell Comprising Electrode Lead Having Gas Adsorbent
US6984471B2 (en) Nonaqueous electrolyte and nonaqueous electrolyte battery
US11342553B2 (en) Methods for prelithiation of silicon containing electrodes
US20220166017A1 (en) Electrodes and electrochemical cells including a dendrite inhibitor protective coating
US20130236757A1 (en) Cell assemblies with neutral cases
US20220181629A1 (en) Elastic binding polymers for electrochemical cells
US20220344669A1 (en) Current collectors having surface structures for controlling formation of solid-electrolyte interface layers
JP5426809B2 (en) Secondary battery, electronic equipment using secondary battery and transportation equipment
JP5023649B2 (en) Lithium ion secondary battery
KR20130131983A (en) Secondary battery comprising apparatus for preventing overcharge
US20200076000A1 (en) Non-aqueous electrolyte and non-aqueous electrolyte secondary battery
US20220367848A1 (en) Double-sided electrodes and electrochemical cells including the same

Legal Events

Date Code Title Description
AS Assignment

Owner name: PELLION TECHNOLOGIES INC., MASSACHUSETTS

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:DOWNIE, CRAIG;DOE, ROBERT ELLIS;EAGLESHAM, DAVID;REEL/FRAME:046977/0438

Effective date: 20180801

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

Free format text: DOCKETED NEW CASE - READY FOR EXAMINATION

AS Assignment

Owner name: VIKING POWER SYSTEMS PTE. LTD, SINGAPORE

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:PELLION TECHNOLOGIES, INC.;REEL/FRAME:050644/0024

Effective date: 20190813

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: RESPONSE AFTER FINAL ACTION FORWARDED TO EXAMINER

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: NON FINAL ACTION MAILED

STCB Information on status: application discontinuation

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