US20100255376A1 - Gas phase deposition of battery separators - Google Patents

Gas phase deposition of battery separators Download PDF

Info

Publication number
US20100255376A1
US20100255376A1 US12/728,157 US72815710A US2010255376A1 US 20100255376 A1 US20100255376 A1 US 20100255376A1 US 72815710 A US72815710 A US 72815710A US 2010255376 A1 US2010255376 A1 US 2010255376A1
Authority
US
United States
Prior art keywords
separator
component
porous
layer
electrode
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
US12/728,157
Inventor
Benjamin Park
Alexander Gorkovenko
Rabih Zaouk
William Schank
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.)
Enevate Corp
Original Assignee
Carbon Micro Battery Corp
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 Carbon Micro Battery Corp filed Critical Carbon Micro Battery Corp
Priority to US12/728,157 priority Critical patent/US20100255376A1/en
Assigned to CARBON MICRO BATTERY CORPORATION reassignment CARBON MICRO BATTERY CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: GORKOVENKO, ALEXANDER, PARK, BENJAMIN, ZAOUK, RABIH, SCHANK, WILLIAM
Publication of US20100255376A1 publication Critical patent/US20100255376A1/en
Assigned to ENOVATE CORPORATION reassignment ENOVATE CORPORATION CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: CARBON MICRO BATTERY CORPORATION
Assigned to ENEVATE CORPORATION reassignment ENEVATE CORPORATION CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: ENOVATE CORPORATION
Priority to US13/740,050 priority patent/US8603683B2/en
Priority to US14/069,125 priority patent/US9647259B2/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
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/04Processes of manufacture in general
    • H01M4/0471Processes of manufacture in general involving thermal treatment, e.g. firing, sintering, backing particulate active material, thermal decomposition, pyrolysis
    • 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
    • H01M4/133Electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
    • 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
    • H01M4/58Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
    • H01M4/583Carbonaceous material, e.g. graphite-intercalation compounds or CFx
    • 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
    • H01M50/411Organic material
    • H01M50/414Synthetic resins, e.g. thermoplastics or thermosetting resins
    • 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
    • H01M50/46Separators, membranes or diaphragms characterised by their combination with electrodes
    • 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

  • Embodiments of the present disclosure relate to battery separators.
  • further embodiments relate to deposition of battery separators.
  • a battery typically includes a separator and/or electrolyte between an anode and a cathode.
  • FIG. 1 illustrates a separator 13 sandwiched between an anode 14 and a cathode 12 .
  • FIG. 1 further illustrates a load 11 electrically connected to the anode 14 and the cathode 12 to form a battery 10 in a discharge configuration. The load can be replaced with a charger to have the battery 10 in a charging configuration.
  • the separator is generally a film material, made of an electrically insulating polymer that prevents electrons from flowing from anode to cathode. Separators are porous to allow ions to pass through the separator.
  • the separator, cathode and anode materials are individually formed into sheets, films, or active material coated foils. Sheets of the cathode, separator and anode are subsequently stacked or rolled with the separator separating the cathode and anode to form the battery.
  • a separator in prior art batteries is a sheet and therefore, is limited to specific manufacturing methods (e.g., mainly winding methods and stacking). In these methods, the anodes and cathodes (e.g., electrodes) are usually films.
  • a method of making a battery separator includes gas phase depositing a composition onto an electrode.
  • the composition comprising a first component selected from the group consisting of polymers, dimers and monomers, and a second component selected from the group consisting of polymers, dimers and monomers.
  • the first component being different than the second component.
  • the first component and the second component each form separate polymer phases and together form a layer.
  • the method further includes removing at least a portion of the second component to form a porous separator layer.
  • the method further includes activating a first dimer and pyrolysing the first dimer to form the first component, and activating a second dimer and pyrolysing the second dimer to form the second component.
  • a method of making a battery separator includes gas phase depositing a composition onto an electrode.
  • the composition comprising a first component selected from the group consisting of polymers, dimers and monomers.
  • the method further includes forming a first polymer from the first component to form a layer comprising the first polymer and a second component selected from the group consisting of by-products and remaining portions of the first component from the forming the first polymer.
  • the method also further includes removing at least a portion of the second component to form a porous separator layer.
  • a method of making a battery separator includes forming a first layer onto an electrode, the first layer comprising a porous template, and gas phase depositing a first component into the porous template.
  • the porous template can include a removable material.
  • the first component selected from the group consisting of polymers, dimers and monomers.
  • the method further includes removing at least a portion of the porous template to form a porous separator layer comprising the first component.
  • a method of making a battery separator includes gas phase depositing a composition onto an electrode.
  • the composition comprises a precursor and a foaming agent.
  • the method further includes evaporating the foaming agent to foam the precursor, and polymerizing the precursor to form a porous separator layer.
  • a battery separator having a gas phase deposited porous separator is provided.
  • the porous separator has an open cell structure.
  • the porous separator comprises parylene.
  • a battery separator includes a gas phase deposited nonporous separator, wherein the nonporous separator can absorb a liquid electrolyte is provided.
  • the nonpourous separator can be gelled.
  • a battery in another embodiment, includes a gas phase deposited separator deposited on an electrode is provided.
  • the gas phase deposited separator can be a polymer.
  • the electrode can be a material that reacts with or absorbs ions.
  • the electrode comprises carbon.
  • the battery can be a lithium ion battery or a fluoride battery.
  • the gas phase deposited separator comprises an open cell structure.
  • a battery electrode and separator includes an electrode comprising at least one cavity or protrusion on at least one surface of the electrode.
  • the cavity or protrusion can have a length greater than about 5 mils and at least one width that is less than about 5 mils.
  • the battery electrode and separator further includes a substantially conformal separator layer gas phase deposited onto a surface of the at least one cavity or protrusion.
  • the length of the cavity or protrusion is between about 5 and 100 mils, and the at least one width of the cavity or protrusion is between about 1 and 5 mils.
  • FIG. 1 illustrates a separator sandwiched between an anode and a cathode to form a battery.
  • FIG. 2 illustrates a separator deposited onto a complex shaped first electrode with a second electrode deposited onto or sandwiched against the separator to form a battery.
  • FIG. 3 illustrates one embodiment of a separator deposition process.
  • FIG. 4 illustrates pyrolysis of di-para-xylylene to form para-xylylene and subsequent polymerization of para-xylylene.
  • FIG. 5 illustrates a porous separator deposited on a substrate.
  • FIG. 6 illustrates a conformal porous separator deposited on a non-planar substrate.
  • the separator is deposited onto an electrode (e.g. cathode or anode).
  • a deposited separator can be deposited on complex shaped electrodes. For example, FIG.
  • FIG. 2 illustrates a separator 23 that can be deposited onto a complex shaped first electrode that including either an anode 24 or a cathode 22 .
  • a second electrode can be deposited onto the separator 23 or can be sandwiched against the separator 23 .
  • the first electrode can have a deposited separator 23 which can then be fitted, mated, or coupled together with the second electrode.
  • the first electrode and second electrode can be configured to sandwich the separator when fitted, mated, or coupled together.
  • a battery 20 can be formed from the separator 23 , anode 24 and cathode 22 .
  • the battery can be put into a discharge configuration by putting a load 21 into electrical communication with the anode 24 and cathode 22 or can be put into a charge configuration by putting a charger into electrical communication with the anode 24 and cathode 22 .
  • the parameters of deposition can be adjusted to deposit a separator with porosity.
  • the porosity of the separator can be adjusted for optimal performance of the battery. For example, the morphology, size, shape, volume percent, etc. can be adjusted.
  • the separator has an open cell structure.
  • gas phase deposition can be used to deposit the separator.
  • the separator can be a separator in a lithium ion battery or a fluoride ion battery.
  • the anode can be a material that reacts with or absorbs ions (e.g. battery active material).
  • carbon can be used as the anode and the separator can be deposited directly on the carbon.
  • Depositing paraxylylene film on carbon is discussed in United States Patent Publication No. 2008/0241593. Some embodiments include depositing a polymer that is any of one or more of the group of polymers, dimers or monomers which can be deposited in a conformal coating by vapor deposition, chemical vapor deposition, initiated chemical vapor deposition, fumed deposition, etc. Process parameters can be selected to produce a conformal separator layer on a non-planar surface.
  • the battery includes a liquid or gel electrolyte.
  • the separator preferably does not dissolve in typical battery electrolytes such as compositions that include: Ethylene Carbonate (EC), Propylene Carbonate (PC), Dimethyl Carbonate (DMC), Ethyl Methyl Carbonate (EMC), Diethyl Carbonate (DEC), etc. with dissolved LiBF 4 , LiAsF 6 , LiPF 6 , and LiClO 4 etc.
  • the separator is wet or soaked with a liquid or gel electrolyte.
  • the separator preferably does not melt below about 100 to 120° C.
  • the separator should also have sufficient mechanical properties.
  • a battery, in operation can experience expansion and contraction of the anode and/or the cathode.
  • the separator can expand and contract by at least about 5 to 10% without failing.
  • the separator can also be flexible.
  • the separator is a polymer.
  • the separator is parylene.
  • the parylene can be any of the various types such as for example parylene N, parylene C, parylene D, parylene F, etc.
  • gas phase deposition 100 of the polymer can be done by first activating, block 101 , a dimer such as di-para-xylylene 201 as illustrated in FIG. 2 . Activation can be performed at about 170 to 200° C. so that the dimer vaporizes (e.g. sublimation). The vaporized dimer then is cleaved by pyrolysis, block 102 , to form monomers such as para-xylylene 202 as illustrated in FIG.
  • Cleaving of the dimer can be done in a pyrolysis furnace at about 600 to 700° C. and typically at about 675° C.
  • the monomer is then deposited, block 103 , on a substrate surface and can chemically react with other monomers to form a polymer such as poly-para-xylylene 203 as illustrated in FIG. 4 .
  • depositing the separator allows the substrate (e.g. electrode) to have complex shapes. Examples of parylene deposition techniques are discussed in J. B. Fortin et al., “A Model for the Chemical Vapor Deposition of Poly(para-xylylene) (Parylene) Thin Films,” Chem. Mater. 2002, 14, 1945-1949 and U.S. Pat. No. 6,946,406.
  • the parameters of deposition can be adjusted to change the porosity and uniformity of the deposited separator.
  • the separator should be sufficiently porous so that ions can pass through the separator once wet with, for example, a liquid or gel electrolyte. Alternatively, the separator could absorb the electrolyte through a gelling or other process even without significant porosity. In one embodiment, the separator does not have significant porosity, but can be gelled or otherwise absorb a liquid electrolyte. In another embodiment, the separator has no porosity, but can be gelled or otherwise absorb a liquid electrolyte. On the other hand, a porous separator should also not be too porous to allow the anode and cathode to transfer electrons through the separator.
  • oblique angle deposition techniques e.g. glancing angle deposition
  • Another technique involves depositing with the substrate at relatively low temperatures (e.g. below room temperature). Examples of depositing Parylene-N films at liquid nitrogen temperatures are discussed in J. Erjavec et al., “Novel Parylene-N films deposited at liquid nitrogen temperatures,” Materials Letters 39 (1999) 339-342.
  • Other parameters of the deposition process can be adjusted such as the composition of the deposited polymer and the deposition temperature. The composition and/or deposition temperature can be varied during deposition.
  • Deposition temperatures can include for example, atmospheric temperature, substrate temperature, pyrolysis temperature, etc. In one embodiment, at least one deposition temperature is raised during deposition, and in another embodiment, at least one deposition temperature is lowered during deposition.
  • the atmosphere in the deposition chamber can also be adjusted. For example, the level of vacuum or the amount of pressure can be adjusted. In one embodiment, deposition is done in a relatively low pressure (e.g. vacuum or below atmospheric pressure). In some embodiments, a gas is used. In one embodiment, the gas in the chamber can be a relatively inert gas (e.g. argon). In some embodiments, the deposition pressure is relatively high (e.g. above atmospheric pressure). In additional embodiments, the deposition rate is adjusted. In one embodiment, the deposition rate is increased during deposition, and in another embodiment, the deposition rate is decreased during deposition.
  • a method of making a battery separator can include gas phase depositing a composition onto an electrode.
  • the composition can include a first component selected from the group consisting of polymers, dimers and monomers, a second component selected from the group consisting of polymers, dimers and monomers, and the first component being different than the second component.
  • the first component and the second component each form separate polymer phases and together form a layer.
  • the concentration of one component is higher than another component.
  • the concentration of a component is varied relative to another component during deposition.
  • one or more components can be monomers. In one embodiment, both monomers are cleaved at similar temperatures so that the monomers can be formed in the same step.
  • the monomers can be cleaved in separate steps and mixed during deposition.
  • Parylene in some embodiments, can be deposited with dibenzyl or stilbene. Parylene, dibenzyl and stilbene all cleave at similar temperatures. In one embodiment, concentration of parylene is lower than dibenzyl or stilbene. In another embodiment, concentration of parylene is higher than dibenzyl or stilbene.
  • a method includes activating a first dimer and pyrolysing the first dimer to form the first component, and activating a second dimer and pyrolysing the second dimer to form the second component. After deposition, one of the two deposited components can be removed to form a porous polymer layer.
  • a method includes removing at least a portion of the second component to form a porous separator layer.
  • the component to be removed can be dissolved in a solvating solution and/or removed by other chemical or mechanical processes.
  • the pressure around the components can be increased (e.g. decrease vacuum).
  • dibenzyl or stilbene is removed to leave a parylene porous separator.
  • a method of making a battery separator includes gas phase depositing a composition onto an electrode.
  • the composition can include a first component selected from the group consisting of polymers, dimers and monomers. In another embodiment, only one dimer type is used.
  • the method can include forming a first polymer from the first component to form a layer comprising the first polymer and a second component selected from the group consisting of by-products and remaining portions of the first component from the forming the first polymer.
  • the dimers not all dimers are cleaved to form monomers and/or monomers further decompose into by-products. The dimers and by-products deposit with the monomers.
  • the method can include removing at least a portion of the second component to form a porous separator layer.
  • the deposited layer can be subsequently heat treated to release the dimers and by-products to form a porous structure. Examples of forming porous layers are discussed in Y. S. Yeh et al., “Polymerization of Para-xylylene Derivatives” J. Polymer Sci.: Part B: Polymer Physics, Vol. 28, 545-568 (1990).
  • the pyrolsis temperature is relatively high (e.g. above about 675° C.). In another embodiment, the pyrolsis temperature is relatively low (e.g. below about 675° C.).
  • a template approach can be used.
  • a porous template layer can be deposited on a substrate.
  • a method of making a battery separator can include forming a first layer onto an electrode, the first layer includes a porous template, and gas phase depositing a first component into the porous template.
  • the porous template can be a removable material.
  • the first component can be selected from the group consisting of polymers, dimers and monomers.
  • a polymer such as parylene can be used to fill the porosity in the porous template layer.
  • the method can further include removing at least a portion of the porous template to form a porous separator layer comprising the first component.
  • the porous template layer can then be removed leaving a porous polymer layer.
  • the template layer is removed with a solution.
  • the template layer is removed by evaporation.
  • the porous separator should substantially remain after removal of the template layer.
  • the porous separator has an open cell structure.
  • the open cell structure allows ions to transfer through the porous separator.
  • An illustration of porous structure is shown in FIG. 5 where a porous separator 301 is deposited on a substrate 302 and has porosity 303 .
  • a porous separator has a conformal thickness.
  • the porous separator should have a sufficiently conformal thickness such that the electrochemical potential across the porous separator is substantially uniform.
  • the overall thickness of the porous separator can also be selected based on properties and porosity of the separator.
  • FIG. 6 illustrates a conformal porous separator 401 deposited on non-planar substrate surface 402 .
  • the deposition techniques described above can be used to produce a conformal porous separator or a substantially conformal porous separator.
  • the porous separator can have a substantially uniform thickness.
  • the electrode includes cavities (e.g., grooves, pores, and pits) and/or protrusions (e.g. bumps and ridges).
  • a separator made from a film material may not be able to contact the electrode inside of the cavities and may not be able to contact the electrode on the protrusions and valleys or depressions between protrusions.
  • gas phase depositing a separator can deposit the separator onto the surfaces within the cavities and onto protrusions and valleys.
  • a separator can be gas phase deposited onto a rough surface or a surface with rigosity.
  • a battery electrode and separator includes a substantially conformal separator layer gas phase deposited onto a surface of the at least one cavity or protrusion.
  • the cavity or protrusion has a length of at least about 5 mils (127 ⁇ m) or a length of about 5 mils (127 ⁇ m) to about 100 mils (2.54 mm).
  • the cavity or protrusion can also have a width.
  • the width may be oblong.
  • the cavity or protrusion can have a first width larger than a second width such as, for example, a groove or ridge.
  • the cavity or protrusion has at least one width that is less than about 100 mils (2.54 mm), at lest one width that is less than about 5 mils (127 ⁇ m), or at least one width that is about 1 mil (25.4 ⁇ m) to about 5 mils (127 ⁇ m).
  • the length is larger than at least one width of the cavity or protrusion.
  • the cavities or protrusions have a smallest dimension less than 5 mils (127 ⁇ m) or between about 1 mil (25.4 ⁇ m) to about 5 mils (127 ⁇ m).
  • the smallest dimension can include, for example, the at least one width or the length.
  • a substantially planar surface includes cavities in or protrusions on the surface.
  • the porous separator is deposited by atomic layer deposition (ALD).
  • ALD atomic layer deposition
  • ALD has two or more precursors.
  • a first precursor and a second precursor can be deposited in series.
  • the deposition of the first precursor is self-limiting due to a self-terminating surface reactions resulting in a single layer of the first precursor.
  • a second precursor is deposited on the first precursor.
  • the deposition of the second precursor is also self-limiting resulting in a single layer of the second precursor.
  • Deposition of the first precursor and the second precursor can be repeated to produce a multi-layered structure comprising alternating layers of the first precursor and the second precursor.
  • the deposition chamber is purged between deposition of the first precursor and deposition of the second precursor.
  • ALD is that the layer thickness can be substantially conformal. In some embodiments, the layer thickness is substantially atomically conformal. Typical materials that can be deposited by ALD are oxides, metal nitrides, metals and metal sulfides. In some embodiments, ALD is used to deposit on and/or in a porous template layer. The porous template layer can subsequently be removed to leave an ALD deposited porous separator.
  • the porous separator is deposited by plasma deposition.
  • silicon oxide e.g. SiO x
  • a composition is injected into plasma.
  • the composition can include one or more precursors.
  • the precursor can be mixed with a gas before or during injection into the plasma.
  • the gas can be a relatively inert gas (e.g. argon).
  • the precursor can be, for example, Bis(trimethylsilyl)amine (e.g. hexamethyldisilazane or HMDS) or Bis(trimethylsilyl) oxide (e.g. Hexamethyldisiloxane or HMDSO).
  • the plasma ionizes (e.g. dissociates) the precursor.
  • the dissociated precursor can then be deposited onto a substrate.
  • An example of plasma deposition is discussed in J. Schafer et al., “Local deposition of SiO x plasma polymer films by miniaturized atmospheric pressure plasma jet (APPJ),” J. Phys. D: Appl. Phys. 41 (2008) 194010.
  • two or more precursors are introduced into the plasma together or sequentially. After the precursors are deposited, one or more precursors can be removed. The precursors to be removed can be dissolved in a solvating solution and/or removed by other chemical or mechanical processes. The remaining one or more precursors form a porous structure.
  • the composition injected into the plasma includes a concentration of one precursor greater than another precursor.
  • the concentration of the precursor to be removed is greater than the concentration of the precursor that will remain as the porous separator. In other embodiments, the concentration of the precursor to be removed is less than the concentration of the precursor that will remain. In another embodiment, the precursors are in equal concentrations.
  • the composition and/or deposition temperature is varied during the plasma deposition. For example, at least one deposition temperature is raised ruing deposition, and in another example, at least one deposition temperature is lowered during deposition.
  • the atmosphere in the deposition chamber can also be adjusted. For example, the level of vacuum or the amount of pressure can be adjusted. In one embodiment, deposition is done in a relatively low pressure (e.g. vacuum or below atmospheric pressure). In some embodiments, the deposition pressure is relatively high (e.g.
  • the deposition rate is adjusted. In one embodiment, the deposition rate is increased during deposition, and in another embodiment, the deposition rate is decreased during deposition. In some embodiments, plasma deposition is used to make a porous template layer. In other embodiments, plasma deposition is used to deposit on and/or in a porous template layer.
  • the porous separator is deposited by a droplet spray.
  • the droplet spray can be airless or include air.
  • the size of the droplets are about 3 to 4.2 ⁇ m. In another embodiment, the size of the droplets are less than about 5 ⁇ m. In a further embodiment, the size of the droplets are small enough to get into topographical features of a substrate.
  • the porous separator is produced by depositing and foaming a composition.
  • a method of making a battery separator includes gas phase depositing a composition onto an electrode.
  • the composition comprises a precursor and a foaming agent.
  • Deposition of the composition can be by, for example, thermal vapor deposition.
  • the composition can include one or more precursors.
  • the precursor is a monomer.
  • the monomer can be a cyanoacrylate (e.g. ethyl-2-cyanoacrylate), methyl methacrylate (MMA), methyl vinyl ether or ethyl vinyl ether.
  • only one type of monomer is used as the precursor. In other embodiments, more than one type of monomer is used as the precursor.
  • the composition can also include a solvent that the monomer can be dissolved in.
  • cyanoacrylate can be dissolved in ethereal solvents (e.g. tetrahydrofuran (THF)).
  • the composition includes a foaming agent.
  • Foaming agents can include pentane, hexane, 1,1,2-trichlorotriflouroethane, cyclohexane, petroleum ether, diethyl ether, etc.
  • the method can include evaporating the foaming agent to foam the precursor, and polymerizing the precursor to form a porous separator layer. Foaming of the composition can be done during or after deposition of the composition.
  • the deposition and foaming can be done in the same chamber or different chambers.
  • an initiator polymerizes the monomer.
  • Initiators can include H 2 O, N,N-dimethyl-p-toluidine, N-(oxydiethylene)benzothiazole-2-sulfenamide, etc.
  • Introduction of the initiator to the composition can be done during deposition or after deposition of the composition.
  • the initiator can be introduced in the same chamber as the deposition or in a different chamber.
  • the polymerization of the monomer creates heat which causes the foaming agent to evaporate resulting in foaming.
  • a separate heat source heats the composition to cause the foaming agent to evaporate.
  • a vacuum is pulled to cause the foaming agent to evaporate.
  • Further polycyanoacrylate foaming details are discussed in International Publication No. WO 92/09651 and U.S. Pat. No. 7,323,207.
  • the composition has a concentration of precursor greater than a concentration of foaming agent.
  • the composition has a concentration of foaming agent greater than of precursor.
  • the precursor and foaming agent are in equal concentrations.
  • the foaming process produces a substantially conformal porous separator.
  • the foamed porous layer is an open-porous structure.
  • Some polymers may dissolve in typical battery electrolytes.
  • Cross-linking the polymer can improve the polymer's ability to resist dissolving in battery electrolytes.
  • Cross-linking can also add mechanical stability. However, too much cross-linking may inhibit ion conduction.
  • Double-functional chemicals can be used for cross-linking.
  • N,N-methyl-bisacrylamide can be used to cross-link polycyanoacrylate.
  • Other cross-linking agents e.g. double-, triple-, and other functional groups
  • a radical initiator e.g. radical catalyst
  • Radical initiator examples include butanone peroxide and benzoyl peroxide.
  • An amine activator for example N,N-dimethyl-p-toluidine, may be used in combination with radical initiator for initiating polymerization.
  • a stabilizer may be used in some embodiments to prevent anionic initiation.
  • stabilizes can include acids.
  • cross-linking agents, radical initiators, amine activators and stabilizers are discussed in U.S. Pat. No. 3,940,362.
  • a polymer is produced using a mixture of monomer and cross-linking agent.
  • a polymer is produced using a mixture of monomer, cross-linking agent and radical initiator.
  • a polymer is produced using a mixture of monomer, cross-linking agent, radical initiator and amine activator.
  • the mixture includes MMA, a crosslinking agent (e.g. 1,6-Hexanediol Diacrylate, trimethylolpropane triacrylate, ethylene glycol dimethacrylate), radical initiator (e.g. benzoyl peroxide) and amine activator (e.g. N,N-dimethyl-p-toluidine).
  • the ratio of MMA to crosslinking agent is between about 8 to 1 and about 1 to 1.
  • the radical initiator and the amine activator are each about 5 percent of the mixture.
  • Polymerization systems may be radical initiation systems or cationic polymerization systems. Mixtures that include cyanoacrylate or MMA are radical initiation systems.
  • Cationic polymerization systems include methyl vinyl ether or ethyl vinyl ether as the monomer. Cationic polymerization systems can also include a cross-linking agent (e.g. divinyl ether of ethylene glycol) and an initiator (e.g. BF 3 ).
  • a cross-linking agent e.g. divinyl ether of ethylene glycol
  • an initiator e.g. BF 3
  • the foamed porous layer can be used as a template for the porous separator.
  • the porosity of the foamed porous layer can be filled with a material that will be the porous separator. After the foamed porous layer is filled with the material, the foamed porous layer is removed. For example, the foamed porous layer can be chemically or mechanically removed.

Abstract

In certain embodiments, a gas phase deposited porous separator is provided. The porous separator can be deposited onto an electrode. The electrode can include at least one cavity or protrusion, and the separator layer can be gas phase deposited onto a surface of the at least one cavity or protrusion. In certain embodiments, a method of gas phase depositing a separator layer is provided.

Description

    CROSS-REFERENCE TO RELATED APPLICATIONS
  • This application claims the benefit of U.S. Provisional Application Nos. 61/161,740, filed Mar. 19, 2009, 61/168,194, filed Apr. 9, 2009, and 61/226,217, filed Jul. 16, 2009, the entirety of each of which is hereby incorporated by reference.
  • BACKGROUND
  • 1. Field
  • Embodiments of the present disclosure relate to battery separators. In particular, further embodiments relate to deposition of battery separators.
  • 2. Description of the Related Art
  • A battery typically includes a separator and/or electrolyte between an anode and a cathode. FIG. 1 illustrates a separator 13 sandwiched between an anode 14 and a cathode 12. FIG. 1 further illustrates a load 11 electrically connected to the anode 14 and the cathode 12 to form a battery 10 in a discharge configuration. The load can be replaced with a charger to have the battery 10 in a charging configuration. In one class of batteries, the separator is generally a film material, made of an electrically insulating polymer that prevents electrons from flowing from anode to cathode. Separators are porous to allow ions to pass through the separator. Typically, the separator, cathode and anode materials are individually formed into sheets, films, or active material coated foils. Sheets of the cathode, separator and anode are subsequently stacked or rolled with the separator separating the cathode and anode to form the battery. A separator in prior art batteries is a sheet and therefore, is limited to specific manufacturing methods (e.g., mainly winding methods and stacking). In these methods, the anodes and cathodes (e.g., electrodes) are usually films.
  • SUMMARY
  • In certain embodiments, a method of making a battery separator includes gas phase depositing a composition onto an electrode. The composition comprising a first component selected from the group consisting of polymers, dimers and monomers, and a second component selected from the group consisting of polymers, dimers and monomers. The first component being different than the second component. The first component and the second component each form separate polymer phases and together form a layer. The method further includes removing at least a portion of the second component to form a porous separator layer. In certain embodiments, the method further includes activating a first dimer and pyrolysing the first dimer to form the first component, and activating a second dimer and pyrolysing the second dimer to form the second component.
  • In further embodiments, a method of making a battery separator includes gas phase depositing a composition onto an electrode. The composition comprising a first component selected from the group consisting of polymers, dimers and monomers. The method further includes forming a first polymer from the first component to form a layer comprising the first polymer and a second component selected from the group consisting of by-products and remaining portions of the first component from the forming the first polymer. The method also further includes removing at least a portion of the second component to form a porous separator layer.
  • In one embodiment, a method of making a battery separator includes forming a first layer onto an electrode, the first layer comprising a porous template, and gas phase depositing a first component into the porous template. The porous template can include a removable material. The first component selected from the group consisting of polymers, dimers and monomers. The method further includes removing at least a portion of the porous template to form a porous separator layer comprising the first component.
  • In some embodiments, a method of making a battery separator includes gas phase depositing a composition onto an electrode. The composition comprises a precursor and a foaming agent. The method further includes evaporating the foaming agent to foam the precursor, and polymerizing the precursor to form a porous separator layer.
  • In an embodiment, a battery separator having a gas phase deposited porous separator is provided. In some embodiments, the porous separator has an open cell structure. In further embodiments, the porous separator comprises parylene.
  • In one embodiment, a battery separator includes a gas phase deposited nonporous separator, wherein the nonporous separator can absorb a liquid electrolyte is provided. In some embodiments, the nonpourous separator can be gelled.
  • In another embodiment, a battery includes a gas phase deposited separator deposited on an electrode is provided. The gas phase deposited separator can be a polymer. The electrode can be a material that reacts with or absorbs ions. In some embodiments, the electrode comprises carbon. The battery can be a lithium ion battery or a fluoride battery. In some embodiments, the gas phase deposited separator comprises an open cell structure.
  • In a further embodiment, a battery electrode and separator includes an electrode comprising at least one cavity or protrusion on at least one surface of the electrode. The cavity or protrusion can have a length greater than about 5 mils and at least one width that is less than about 5 mils. The battery electrode and separator further includes a substantially conformal separator layer gas phase deposited onto a surface of the at least one cavity or protrusion. In certain embodiments, the length of the cavity or protrusion is between about 5 and 100 mils, and the at least one width of the cavity or protrusion is between about 1 and 5 mils.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • FIG. 1 illustrates a separator sandwiched between an anode and a cathode to form a battery.
  • FIG. 2 illustrates a separator deposited onto a complex shaped first electrode with a second electrode deposited onto or sandwiched against the separator to form a battery.
  • FIG. 3 illustrates one embodiment of a separator deposition process.
  • FIG. 4 illustrates pyrolysis of di-para-xylylene to form para-xylylene and subsequent polymerization of para-xylylene.
  • FIG. 5 illustrates a porous separator deposited on a substrate.
  • FIG. 6 illustrates a conformal porous separator deposited on a non-planar substrate.
  • DETAILED DESCRIPTION
  • To be able to build a battery with film type electrodes and/or more complex shaped electrodes, another technique to produce the separator is described herein. By using a complex shaped electrode, the electrode may not need to be rolled as in a conventional wound battery to provide sufficient surface area between the electrodes and the separator. Therefore, electrode materials that may not have sufficient deformability to be able to be rolled may be used. For example, carbon in a solid form (e.g. not carbon powder with a binder) can be used. In some embodiments, the separator is deposited onto an electrode (e.g. cathode or anode). Advantageously, a deposited separator can be deposited on complex shaped electrodes. For example, FIG. 2 illustrates a separator 23 that can be deposited onto a complex shaped first electrode that including either an anode 24 or a cathode 22. A second electrode can be deposited onto the separator 23 or can be sandwiched against the separator 23. For example, the first electrode can have a deposited separator 23 which can then be fitted, mated, or coupled together with the second electrode. The first electrode and second electrode can be configured to sandwich the separator when fitted, mated, or coupled together. A battery 20 can be formed from the separator 23, anode 24 and cathode 22. Furthermore, the battery can be put into a discharge configuration by putting a load 21 into electrical communication with the anode 24 and cathode 22 or can be put into a charge configuration by putting a charger into electrical communication with the anode 24 and cathode 22.
  • The parameters of deposition can be adjusted to deposit a separator with porosity. The porosity of the separator can be adjusted for optimal performance of the battery. For example, the morphology, size, shape, volume percent, etc. can be adjusted. In one embodiment, the separator has an open cell structure. In some embodiments, gas phase deposition can be used to deposit the separator. The separator can be a separator in a lithium ion battery or a fluoride ion battery. In some embodiments, the anode can be a material that reacts with or absorbs ions (e.g. battery active material). In one embodiment, carbon can be used as the anode and the separator can be deposited directly on the carbon. Depositing paraxylylene film on carbon is discussed in United States Patent Publication No. 2008/0241593. Some embodiments include depositing a polymer that is any of one or more of the group of polymers, dimers or monomers which can be deposited in a conformal coating by vapor deposition, chemical vapor deposition, initiated chemical vapor deposition, fumed deposition, etc. Process parameters can be selected to produce a conformal separator layer on a non-planar surface.
  • In some embodiments, the battery includes a liquid or gel electrolyte. The separator preferably does not dissolve in typical battery electrolytes such as compositions that include: Ethylene Carbonate (EC), Propylene Carbonate (PC), Dimethyl Carbonate (DMC), Ethyl Methyl Carbonate (EMC), Diethyl Carbonate (DEC), etc. with dissolved LiBF4, LiAsF6, LiPF6, and LiClO4 etc. In some embodiments, the separator is wet or soaked with a liquid or gel electrolyte. In addition, the separator preferably does not melt below about 100 to 120° C. The separator should also have sufficient mechanical properties. A battery, in operation, can experience expansion and contraction of the anode and/or the cathode. Preferably, the separator can expand and contract by at least about 5 to 10% without failing. The separator can also be flexible.
  • In some embodiments, the separator is a polymer. In one embodiment, the separator is parylene. The parylene can be any of the various types such as for example parylene N, parylene C, parylene D, parylene F, etc. As illustrated in FIG. 3, gas phase deposition 100 of the polymer can be done by first activating, block 101, a dimer such as di-para-xylylene 201 as illustrated in FIG. 2. Activation can be performed at about 170 to 200° C. so that the dimer vaporizes (e.g. sublimation). The vaporized dimer then is cleaved by pyrolysis, block 102, to form monomers such as para-xylylene 202 as illustrated in FIG. 2. Cleaving of the dimer can be done in a pyrolysis furnace at about 600 to 700° C. and typically at about 675° C. The monomer is then deposited, block 103, on a substrate surface and can chemically react with other monomers to form a polymer such as poly-para-xylylene 203 as illustrated in FIG. 4. Advantageously, depositing the separator allows the substrate (e.g. electrode) to have complex shapes. Examples of parylene deposition techniques are discussed in J. B. Fortin et al., “A Model for the Chemical Vapor Deposition of Poly(para-xylylene) (Parylene) Thin Films,” Chem. Mater. 2002, 14, 1945-1949 and U.S. Pat. No. 6,946,406.
  • The parameters of deposition can be adjusted to change the porosity and uniformity of the deposited separator. The separator should be sufficiently porous so that ions can pass through the separator once wet with, for example, a liquid or gel electrolyte. Alternatively, the separator could absorb the electrolyte through a gelling or other process even without significant porosity. In one embodiment, the separator does not have significant porosity, but can be gelled or otherwise absorb a liquid electrolyte. In another embodiment, the separator has no porosity, but can be gelled or otherwise absorb a liquid electrolyte. On the other hand, a porous separator should also not be too porous to allow the anode and cathode to transfer electrons through the separator. To deposit a porous polymer layer, a number of techniques can be used. For example, oblique angle deposition techniques (e.g. glancing angle deposition) can be used to form a columnar structure. Another technique involves depositing with the substrate at relatively low temperatures (e.g. below room temperature). Examples of depositing Parylene-N films at liquid nitrogen temperatures are discussed in J. Erjavec et al., “Novel Parylene-N films deposited at liquid nitrogen temperatures,” Materials Letters 39 (1999) 339-342. Other parameters of the deposition process can be adjusted such as the composition of the deposited polymer and the deposition temperature. The composition and/or deposition temperature can be varied during deposition. Deposition temperatures can include for example, atmospheric temperature, substrate temperature, pyrolysis temperature, etc. In one embodiment, at least one deposition temperature is raised during deposition, and in another embodiment, at least one deposition temperature is lowered during deposition. The atmosphere in the deposition chamber can also be adjusted. For example, the level of vacuum or the amount of pressure can be adjusted. In one embodiment, deposition is done in a relatively low pressure (e.g. vacuum or below atmospheric pressure). In some embodiments, a gas is used. In one embodiment, the gas in the chamber can be a relatively inert gas (e.g. argon). In some embodiments, the deposition pressure is relatively high (e.g. above atmospheric pressure). In additional embodiments, the deposition rate is adjusted. In one embodiment, the deposition rate is increased during deposition, and in another embodiment, the deposition rate is decreased during deposition.
  • In some embodiments, more than one component are deposited together. A method of making a battery separator can include gas phase depositing a composition onto an electrode. The composition can include a first component selected from the group consisting of polymers, dimers and monomers, a second component selected from the group consisting of polymers, dimers and monomers, and the first component being different than the second component. The first component and the second component each form separate polymer phases and together form a layer. In one embodiment, the concentration of one component is higher than another component. In some embodiments, the concentration of a component is varied relative to another component during deposition. In some embodiments, one or more components can be monomers. In one embodiment, both monomers are cleaved at similar temperatures so that the monomers can be formed in the same step. In another embodiment, the monomers can be cleaved in separate steps and mixed during deposition. Parylene, in some embodiments, can be deposited with dibenzyl or stilbene. Parylene, dibenzyl and stilbene all cleave at similar temperatures. In one embodiment, concentration of parylene is lower than dibenzyl or stilbene. In another embodiment, concentration of parylene is higher than dibenzyl or stilbene. In certain embodiments, a method includes activating a first dimer and pyrolysing the first dimer to form the first component, and activating a second dimer and pyrolysing the second dimer to form the second component. After deposition, one of the two deposited components can be removed to form a porous polymer layer. In certain embodiments, a method includes removing at least a portion of the second component to form a porous separator layer. For example, the component to be removed can be dissolved in a solvating solution and/or removed by other chemical or mechanical processes. Alternatively, the pressure around the components can be increased (e.g. decrease vacuum). In one embodiment, dibenzyl or stilbene is removed to leave a parylene porous separator. An example of depositing two different monomers to form a porous layer is discussed in United Staes Patent Publication No. 2006/0046044.
  • In further embodiments, a method of making a battery separator includes gas phase depositing a composition onto an electrode. The composition can include a first component selected from the group consisting of polymers, dimers and monomers. In another embodiment, only one dimer type is used. The method can include forming a first polymer from the first component to form a layer comprising the first polymer and a second component selected from the group consisting of by-products and remaining portions of the first component from the forming the first polymer. During pyrolsis of the dimers, not all dimers are cleaved to form monomers and/or monomers further decompose into by-products. The dimers and by-products deposit with the monomers. The method can include removing at least a portion of the second component to form a porous separator layer. For example, the deposited layer can be subsequently heat treated to release the dimers and by-products to form a porous structure. Examples of forming porous layers are discussed in Y. S. Yeh et al., “Polymerization of Para-xylylene Derivatives” J. Polymer Sci.: Part B: Polymer Physics, Vol. 28, 545-568 (1990). In one embodiment, the pyrolsis temperature is relatively high (e.g. above about 675° C.). In another embodiment, the pyrolsis temperature is relatively low (e.g. below about 675° C.).
  • In some embodiments, a template approach can be used. A porous template layer can be deposited on a substrate. A method of making a battery separator can include forming a first layer onto an electrode, the first layer includes a porous template, and gas phase depositing a first component into the porous template. The porous template can be a removable material. The first component can be selected from the group consisting of polymers, dimers and monomers. A polymer such as parylene can be used to fill the porosity in the porous template layer. The method can further include removing at least a portion of the porous template to form a porous separator layer comprising the first component. For example, the porous template layer can then be removed leaving a porous polymer layer. In some embodiments, the template layer is removed with a solution. In other embodiments, the template layer is removed by evaporation. The porous separator should substantially remain after removal of the template layer.
  • In one embodiment, the porous separator has an open cell structure. The open cell structure allows ions to transfer through the porous separator. An illustration of porous structure is shown in FIG. 5 where a porous separator 301 is deposited on a substrate 302 and has porosity 303. Preferably, a porous separator has a conformal thickness. The porous separator should have a sufficiently conformal thickness such that the electrochemical potential across the porous separator is substantially uniform. The overall thickness of the porous separator can also be selected based on properties and porosity of the separator.
  • An advantage of depositing a porous separator onto an electrode (e.g. cathode or anode) is that the electrode can have complex shapes. For example, FIG. 6 illustrates a conformal porous separator 401 deposited on non-planar substrate surface 402. Advantageously, the deposition techniques described above can be used to produce a conformal porous separator or a substantially conformal porous separator. In certain embodiments, the porous separator can have a substantially uniform thickness. In certain embodiments, the electrode includes cavities (e.g., grooves, pores, and pits) and/or protrusions (e.g. bumps and ridges). A separator made from a film material may not be able to contact the electrode inside of the cavities and may not be able to contact the electrode on the protrusions and valleys or depressions between protrusions. Advantageously, gas phase depositing a separator can deposit the separator onto the surfaces within the cavities and onto protrusions and valleys. For example, a separator can be gas phase deposited onto a rough surface or a surface with rigosity. In some embodiments, a battery electrode and separator includes a substantially conformal separator layer gas phase deposited onto a surface of the at least one cavity or protrusion. In certain embodiments, the cavity or protrusion has a length of at least about 5 mils (127 μm) or a length of about 5 mils (127 μm) to about 100 mils (2.54 mm). The cavity or protrusion can also have a width. Furthermore, the width may be oblong. For example, the cavity or protrusion can have a first width larger than a second width such as, for example, a groove or ridge. In certain embodiments, the cavity or protrusion has at least one width that is less than about 100 mils (2.54 mm), at lest one width that is less than about 5 mils (127 μm), or at least one width that is about 1 mil (25.4 μm) to about 5 mils (127 μm). In further embodiments, the length is larger than at least one width of the cavity or protrusion. In certain embodiments, the cavities or protrusions have a smallest dimension less than 5 mils (127 μm) or between about 1 mil (25.4 μm) to about 5 mils (127 μm). The smallest dimension can include, for example, the at least one width or the length. In some embodiments, a substantially planar surface includes cavities in or protrusions on the surface.
  • Many additional deposition techniques can also be used to make a porous separator. In one embodiment, the porous separator is deposited by atomic layer deposition (ALD). Deposition by ALD has two or more precursors. A first precursor and a second precursor can be deposited in series. The deposition of the first precursor is self-limiting due to a self-terminating surface reactions resulting in a single layer of the first precursor. A second precursor is deposited on the first precursor. The deposition of the second precursor is also self-limiting resulting in a single layer of the second precursor. Deposition of the first precursor and the second precursor can be repeated to produce a multi-layered structure comprising alternating layers of the first precursor and the second precursor. Typically, the deposition chamber is purged between deposition of the first precursor and deposition of the second precursor. An advantage of ALD is that the layer thickness can be substantially conformal. In some embodiments, the layer thickness is substantially atomically conformal. Typical materials that can be deposited by ALD are oxides, metal nitrides, metals and metal sulfides. In some embodiments, ALD is used to deposit on and/or in a porous template layer. The porous template layer can subsequently be removed to leave an ALD deposited porous separator.
  • In one embodiment, the porous separator is deposited by plasma deposition. For example, silicon oxide (e.g. SiOx) can be plasma deposited. A composition is injected into plasma. The composition can include one or more precursors. The precursor can be mixed with a gas before or during injection into the plasma. In some embodiments, the gas can be a relatively inert gas (e.g. argon). The precursor can be, for example, Bis(trimethylsilyl)amine (e.g. hexamethyldisilazane or HMDS) or Bis(trimethylsilyl) oxide (e.g. Hexamethyldisiloxane or HMDSO). The plasma ionizes (e.g. dissociates) the precursor. The dissociated precursor can then be deposited onto a substrate. An example of plasma deposition is discussed in J. Schafer et al., “Local deposition of SiOx plasma polymer films by miniaturized atmospheric pressure plasma jet (APPJ),” J. Phys. D: Appl. Phys. 41 (2008) 194010. In some embodiments, two or more precursors are introduced into the plasma together or sequentially. After the precursors are deposited, one or more precursors can be removed. The precursors to be removed can be dissolved in a solvating solution and/or removed by other chemical or mechanical processes. The remaining one or more precursors form a porous structure. In one embodiment, the composition injected into the plasma includes a concentration of one precursor greater than another precursor. In one embodiment, the concentration of the precursor to be removed is greater than the concentration of the precursor that will remain as the porous separator. In other embodiments, the concentration of the precursor to be removed is less than the concentration of the precursor that will remain. In another embodiment, the precursors are in equal concentrations. In one embodiment, the composition and/or deposition temperature is varied during the plasma deposition. For example, at least one deposition temperature is raised ruing deposition, and in another example, at least one deposition temperature is lowered during deposition. The atmosphere in the deposition chamber can also be adjusted. For example, the level of vacuum or the amount of pressure can be adjusted. In one embodiment, deposition is done in a relatively low pressure (e.g. vacuum or below atmospheric pressure). In some embodiments, the deposition pressure is relatively high (e.g. above atmospheric pressure). In additional embodiments, the deposition rate is adjusted. In one embodiment, the deposition rate is increased during deposition, and in another embodiment, the deposition rate is decreased during deposition. In some embodiments, plasma deposition is used to make a porous template layer. In other embodiments, plasma deposition is used to deposit on and/or in a porous template layer.
  • In one embodiment, the porous separator is deposited by a droplet spray. The droplet spray can be airless or include air. In one embodiment, the size of the droplets are about 3 to 4.2 μm. In another embodiment, the size of the droplets are less than about 5 μm. In a further embodiment, the size of the droplets are small enough to get into topographical features of a substrate.
  • In one embodiment, the porous separator is produced by depositing and foaming a composition. In some embodiments, a method of making a battery separator includes gas phase depositing a composition onto an electrode. The composition comprises a precursor and a foaming agent. Deposition of the composition can be by, for example, thermal vapor deposition. The composition can include one or more precursors. In one embodiment, the precursor is a monomer. For example, the monomer can be a cyanoacrylate (e.g. ethyl-2-cyanoacrylate), methyl methacrylate (MMA), methyl vinyl ether or ethyl vinyl ether. In some embodiments, only one type of monomer is used as the precursor. In other embodiments, more than one type of monomer is used as the precursor. The composition can also include a solvent that the monomer can be dissolved in. For example, cyanoacrylate can be dissolved in ethereal solvents (e.g. tetrahydrofuran (THF)). In some embodiments, the composition includes a foaming agent. Foaming agents can include pentane, hexane, 1,1,2-trichlorotriflouroethane, cyclohexane, petroleum ether, diethyl ether, etc. The method can include evaporating the foaming agent to foam the precursor, and polymerizing the precursor to form a porous separator layer. Foaming of the composition can be done during or after deposition of the composition. For example, the deposition and foaming can be done in the same chamber or different chambers. In some embodiments, an initiator polymerizes the monomer. Initiators can include H2O, N,N-dimethyl-p-toluidine, N-(oxydiethylene)benzothiazole-2-sulfenamide, etc. Introduction of the initiator to the composition can be done during deposition or after deposition of the composition. In addition, the initiator can be introduced in the same chamber as the deposition or in a different chamber.
  • In some embodiments, the polymerization of the monomer creates heat which causes the foaming agent to evaporate resulting in foaming. In some embodiments, a separate heat source heats the composition to cause the foaming agent to evaporate. In other embodiments, a vacuum is pulled to cause the foaming agent to evaporate. Further polycyanoacrylate foaming details are discussed in International Publication No. WO 92/09651 and U.S. Pat. No. 7,323,207. In one embodiment, the composition has a concentration of precursor greater than a concentration of foaming agent. In other embodiments, the composition has a concentration of foaming agent greater than of precursor. In a further embodiment, the precursor and foaming agent are in equal concentrations. In some embodiments, the foaming process produces a substantially conformal porous separator. In further embodiments, the foamed porous layer is an open-porous structure.
  • Some polymers may dissolve in typical battery electrolytes. Cross-linking the polymer can improve the polymer's ability to resist dissolving in battery electrolytes. Cross-linking can also add mechanical stability. However, too much cross-linking may inhibit ion conduction. Double-functional chemicals can be used for cross-linking. For example, N,N-methyl-bisacrylamide can be used to cross-link polycyanoacrylate. Other cross-linking agents (e.g. double-, triple-, and other functional groups) include 1,6-Hexanediol Diacrylate, trimethylolpropane triacrylate, ethylene glycol dimethacrylate. A radical initiator (e.g. radical catalyst) can be used along with a cross-linking agent to improve cross-linking. Radical initiator examples include butanone peroxide and benzoyl peroxide. An amine activator, for example N,N-dimethyl-p-toluidine, may be used in combination with radical initiator for initiating polymerization. To improve cross-linking, a stabilizer may be used in some embodiments to prevent anionic initiation. For example, stabilizes can include acids. Further examples of cross-linking agents, radical initiators, amine activators and stabilizers are discussed in U.S. Pat. No. 3,940,362. In one embodiment, a polymer is produced using a mixture of monomer and cross-linking agent. In further embodiments, a polymer is produced using a mixture of monomer, cross-linking agent and radical initiator. In other embodiments, a polymer is produced using a mixture of monomer, cross-linking agent, radical initiator and amine activator. In one embodiment, the mixture includes MMA, a crosslinking agent (e.g. 1,6-Hexanediol Diacrylate, trimethylolpropane triacrylate, ethylene glycol dimethacrylate), radical initiator (e.g. benzoyl peroxide) and amine activator (e.g. N,N-dimethyl-p-toluidine). In some embodiments, the ratio of MMA to crosslinking agent is between about 8 to 1 and about 1 to 1. In some embodiments, the radical initiator and the amine activator are each about 5 percent of the mixture.
  • Polymerization systems may be radical initiation systems or cationic polymerization systems. Mixtures that include cyanoacrylate or MMA are radical initiation systems. Cationic polymerization systems include methyl vinyl ether or ethyl vinyl ether as the monomer. Cationic polymerization systems can also include a cross-linking agent (e.g. divinyl ether of ethylene glycol) and an initiator (e.g. BF3).
  • In one embodiment, the foamed porous layer can be used as a template for the porous separator. The porosity of the foamed porous layer can be filled with a material that will be the porous separator. After the foamed porous layer is filled with the material, the foamed porous layer is removed. For example, the foamed porous layer can be chemically or mechanically removed.
  • Various embodiments have been described above. Although the invention has been described with reference to these specific embodiments, the descriptions are intended to be illustrative and are not intended to be limiting. Various modifications and applications may occur to those skilled in the art without departing from the true spirit and scope of the invention as defined in the appended claims.

Claims (34)

1. A method of making a battery separator comprising:
gas phase depositing a composition onto an electrode, the composition comprising a first component selected from the group consisting of polymers, dimers and monomers and a second component selected from the group consisting of polymers, dimers and monomers, the first component being different than the second component, the first component and the second component each form separate polymer phases and together form a layer; and
removing at least a portion of the second component to form a porous separator layer.
2. The method of claim 1, wherein the first polymer is a substantially continuous phase in the porous layer.
3. The method of claim 1, further comprising:
activating a first dimer; and
pyrolysing the first dimer to form the first component.
4. The method of claim 3, further comprising:
activating a second dimer; and
pyrolysing the second dimer to form the second component.
5. The method of claim 3, wherein the first dimer comprises di-para-xylylene, the first component comprises para-xylylene, and the first polymer comprises parylene.
6. The method of claim 1, wherein the gas phase depositing comprises atomic layer deposition.
7. The method of claim 1, wherein the gas phase depositing comprises plasma deposition.
8. The method of claim 1, wherein the electrode comprises a material that reacts with ions.
9. The method of claim 1, wherein the electrode comprises carbon.
10. The method of claim 1, wherein the porous layer comprises an open cell structure.
11. The method of claim 1, wherein the porous layer comprises parylene.
12. The method of claim 1, wherein the gas phase depositing further comprises reducing the electrode temperature to below room temperature.
13. The method of claim 1, further comprising cross-linking the porous layer.
14. The method of claim 1, wherein the cross-linking the porous layer comprises using at least one cross-linking agent selected from the group consisting of N,N-methyl-bisacrylamide, 1,6-hexanediol diacrylate, trimethylolpropane triacrylate and ethylene glycol dimethacrylate.
15. A method of making a battery separator comprising:
gas phase depositing a composition onto an electrode, the composition comprising a first component selected from the group consisting of polymers, dimers and monomers;
forming a layer comprising a first polymer from the first component and a second component selected from the group consisting of by-products and remaining portions of the first component from the forming the first polymer; and
removing at least a portion of the second component to form a porous separator layer.
16. The method of claim 15, further comprising controlling process parameters to produce the by-products and the remaining portions of the first component.
17. The method of claim 16, wherein the process parameters are controlled to form the layer with about 10 to 90 vol. % of the second component.
18. A method of making a battery separator comprising:
forming a first layer onto an electrode, the first layer comprising a porous template, the porous template comprising a removable material;
gas phase depositing a first component into the porous template, the first component selected from the group consisting of polymers, dimers and monomers; and
removing at least a portion of the porous template to form a porous separator layer comprising the first component.
19. The method of claim 18, further comprising forming a first polymer from the first component.
20. A method of making a battery separator comprising:
gas phase depositing a composition onto an electrode, the composition comprising a precursor and a foaming agent;
evaporating the foaming agent to foam the precursor; and
polymerizing the precursor to form a porous separator layer.
21. The method of claim 20, wherein the evaporating the foaming agent is caused by heat produced from the polymerizing the precursor.
22. The method of claim 20, wherein the evaporating the foaming agent comprises pulling a vacuum.
23. The method of claim 20, wherein the precursor comprises a cyanoacrylate.
24. The method of claim 20, wherein the composition comprises a solvent.
25. The method of claim 20, wherein foaming agent is selected from the group consisting of pentane, hexane, 1,1,2-trichlorotriflouroethane, cyclohexane, petroleum ether and diethyl ether.
26. A battery separator comprising a gas phase deposited porous separator.
27. The battery separator of claim 26, wherein the porous separator has an open cell structure.
28. The battery separator of claim 26, wherein the porous separator comprises parylene.
29. The battery of claim 26, wherein the gas phase deposited separator is a polymer.
30. A battery electrode and separator comprising:
an electrode comprising at least one cavity or protrusion on at least one surface of the electrode, the cavity or protrusion having a length greater than about 5 mils and at least one width that is less than about 5 mils; and
a substantially conformal separator layer gas phase deposited onto a surface of the at least one cavity or protrusion.
31. The battery of claim 30, wherein the length of the cavity or protrusion is between about 5 and 100 mils.
32. The battery of claim 30, wherein the at least one width of the cavity or protrusion is between about 1 and 5 mils.
33. The battery of claim 30, wherein the electrode comprises a material that reacts with or absorbs ions.
34. The battery of claim 30, wherein the electrode comprises carbon.
US12/728,157 2009-03-19 2010-03-19 Gas phase deposition of battery separators Abandoned US20100255376A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
US12/728,157 US20100255376A1 (en) 2009-03-19 2010-03-19 Gas phase deposition of battery separators
US13/740,050 US8603683B2 (en) 2009-03-19 2013-01-11 Gas phase deposition of battery separators
US14/069,125 US9647259B2 (en) 2009-03-19 2013-10-31 Gas phase deposition of battery separators

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US16174009P 2009-03-19 2009-03-19
US16819409P 2009-04-09 2009-04-09
US22621709P 2009-07-16 2009-07-16
US12/728,157 US20100255376A1 (en) 2009-03-19 2010-03-19 Gas phase deposition of battery separators

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US13/740,050 Continuation US8603683B2 (en) 2009-03-19 2013-01-11 Gas phase deposition of battery separators

Publications (1)

Publication Number Publication Date
US20100255376A1 true US20100255376A1 (en) 2010-10-07

Family

ID=42826455

Family Applications (3)

Application Number Title Priority Date Filing Date
US12/728,157 Abandoned US20100255376A1 (en) 2009-03-19 2010-03-19 Gas phase deposition of battery separators
US13/740,050 Active US8603683B2 (en) 2009-03-19 2013-01-11 Gas phase deposition of battery separators
US14/069,125 Active 2032-04-22 US9647259B2 (en) 2009-03-19 2013-10-31 Gas phase deposition of battery separators

Family Applications After (2)

Application Number Title Priority Date Filing Date
US13/740,050 Active US8603683B2 (en) 2009-03-19 2013-01-11 Gas phase deposition of battery separators
US14/069,125 Active 2032-04-22 US9647259B2 (en) 2009-03-19 2013-10-31 Gas phase deposition of battery separators

Country Status (1)

Country Link
US (3) US20100255376A1 (en)

Cited By (36)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012144588A (en) * 2011-01-07 2012-08-02 Univ Of Tokyo Porous membrane, porous structure, method for producing those and sensor
US8603683B2 (en) 2009-03-19 2013-12-10 Enevate Corporation Gas phase deposition of battery separators
CN106159159A (en) * 2015-05-14 2016-11-23 Sk新技术株式会社 Secondary cell composite separating film and preparation method thereof
US9997765B2 (en) 2010-12-22 2018-06-12 Enevate Corporation Electrodes, electrochemical cells, and methods of forming electrodes and electrochemical cells
US20180342734A1 (en) * 2017-05-15 2018-11-29 Millibatt, Inc. Electrolyte material, battery assembly, and production method
US10388943B2 (en) 2010-12-22 2019-08-20 Enevate Corporation Methods of reducing occurrences of short circuits and/or lithium plating in batteries
US10403902B2 (en) 2015-05-15 2019-09-03 Composite Materials Technology, Inc. High capacity rechargeable batteries
US10461366B1 (en) 2010-01-18 2019-10-29 Enevate Corporation Electrolyte compositions for batteries
US10541412B2 (en) 2015-08-07 2020-01-21 Enevate Corporation Surface modification of silicon particles for electrochemical storage
US10603867B1 (en) 2011-05-24 2020-03-31 Enevate Corporation Carbon fibers and methods of producing the same
US10622620B2 (en) 2010-01-18 2020-04-14 Enevate Corporation Methods of forming composite material films
US10680274B2 (en) 2013-03-14 2020-06-09 Enevate Corporation Clamping device for an electrochemical cell stack
US10686214B2 (en) 2017-12-07 2020-06-16 Enevate Corporation Sandwich electrodes and methods of making the same
US10707478B2 (en) 2017-12-07 2020-07-07 Enevate Corporation Silicon particles for battery electrodes
US10763538B2 (en) 2017-12-07 2020-09-01 Enevate Corporation Methods of forming electrochemical cells
US10811727B2 (en) 2017-12-07 2020-10-20 Enevate Corporation Silicon-based energy storage devices with ether containing electrolyte additives
US10847792B2 (en) 2017-12-07 2020-11-24 Enevate Corporation Prelithiated and methods for prelithiating an energy storage device
US10957898B2 (en) 2018-12-21 2021-03-23 Enevate Corporation Silicon-based energy storage devices with anhydride containing electrolyte additives
US10978739B2 (en) 2017-12-07 2021-04-13 Enevate Corporation Silicon-based energy storage devices with carboxylic ether, carboxylic acid based salt, or acrylate electrolyte containing electrolyte additives
US11075408B2 (en) 2017-12-07 2021-07-27 Enevate Corporation Silicon-based energy storage devices with fluorinated polymer containing electrolyte additives
US11133498B2 (en) 2017-12-07 2021-09-28 Enevate Corporation Binding agents for electrochemically active materials and methods of forming the same
US11165099B2 (en) 2018-12-21 2021-11-02 Enevate Corporation Silicon-based energy storage devices with cyclic organosilicon containing electrolyte additives
WO2021221673A1 (en) * 2020-04-30 2021-11-04 Hzo, Inc. Plasma assisted parylene deposition
US11171375B2 (en) 2016-03-25 2021-11-09 Enevate Corporation Stepped electrochemical cells with folded sealed portion
CN114204133A (en) * 2021-12-09 2022-03-18 惠州亿纬锂能股份有限公司 Method for solving expansion of winding type battery cell
US11283069B2 (en) 2017-12-07 2022-03-22 Enevate Corporation Silicon-based energy storage devices with fluorinated cyclic compound containing electrolyte additives
US11374215B2 (en) 2012-08-24 2022-06-28 Sila Nanotechnologies, Inc. Scaffolding matrix with internal nanoparticles
US11380890B2 (en) 2010-01-18 2022-07-05 Enevate Corporation Surface modification of silicon particles for electrochemical storage
US11387443B1 (en) 2021-11-22 2022-07-12 Enevate Corporation Silicon based lithium ion battery and improved cycle life of same
US11398641B2 (en) 2019-06-05 2022-07-26 Enevate Corporation Silicon-based energy storage devices with silicon containing electrolyte additives
US11411249B2 (en) 2017-12-07 2022-08-09 Enevate Corporation Silicon-based energy storage devices with cyclic carbonate containing electrolyte additives
US11411289B2 (en) 2020-08-19 2022-08-09 Millibatt, Inc. Three-dimensional folded battery unit and methods for manufacturing the same
US11515528B2 (en) 2009-09-29 2022-11-29 Georgia Tech Research Corporation Electrodes, lithium-ion batteries, and methods of making and using same
USRE49419E1 (en) 2016-09-01 2023-02-14 Composite Materials Technology, Inc. Nano-scale/nanostructured Si coating on valve metal substrate for lib anodes
US11769870B2 (en) 2009-07-16 2023-09-26 Enevate Corporation Carbon electrode structures for batteries
US11819806B1 (en) * 2018-10-15 2023-11-21 Ampcera Inc. Methods for manufacturing a solid state ionic conductive membrane on a macro porous support scaffold

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101694473B1 (en) * 2014-08-28 2017-01-10 주식회사 엘지화학 A method for manufacturing a separator for a lithium secondary battery and the separator fabricated by the same
KR102324057B1 (en) * 2015-04-23 2021-11-09 에스케이이노베이션 주식회사 Composite Separator and manufacturing method of the same
US9896738B2 (en) * 2015-05-28 2018-02-20 Savannah River Nuclear Solutions, Llc Process for dissolving aluminum for recovering nuclear fuel
US10950846B2 (en) 2019-01-03 2021-03-16 GM Global Technology Operations LLC Method for in situ growth of axial geometry carbon structures in electrodes

Citations (64)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3830733A (en) * 1972-03-09 1974-08-20 Union Carbide Corp Diffusion membranes of controlled permeability,apparatus and process
US3940362A (en) * 1972-05-25 1976-02-24 Johnson & Johnson Cross-linked cyanoacrylate adhesive compositions
US5089360A (en) * 1990-02-08 1992-02-18 Tonen Chemical Corporation High-strength non-woven fabric, method of producing same and battery separator constituted thereby
US5093197A (en) * 1987-12-21 1992-03-03 Entek Manufacturing Inc. Microporous filaments and fibers
US5126219A (en) * 1987-12-21 1992-06-30 Entek Manufacturing Inc. Microporous filaments and fibers, and articles made therefrom
US5230843A (en) * 1987-12-21 1993-07-27 Entek Manufacturing Inc. Process of forming microporous fibers and filaments
US5230949A (en) * 1987-12-21 1993-07-27 Entek Manufacturing Inc. Nonwoven webs of microporous fibers and filaments
US5314765A (en) * 1993-10-14 1994-05-24 Martin Marietta Energy Systems, Inc. Protective lithium ion conducting ceramic coating for lithium metal anodes and associate method
US5332906A (en) * 1992-08-12 1994-07-26 Martin Marietta Energy Systems, Inc. Scintillator assembly for alpha radiation detection and an associated method of making
US5338625A (en) * 1992-07-29 1994-08-16 Martin Marietta Energy Systems, Inc. Thin film battery and method for making same
US5561004A (en) * 1994-02-25 1996-10-01 Bates; John B. Packaging material for thin film lithium batteries
US5569520A (en) * 1994-01-12 1996-10-29 Martin Marietta Energy Systems, Inc. Rechargeable lithium battery for use in applications requiring a low to high power output
US5786396A (en) * 1996-08-21 1998-07-28 Tonen Chemical Corporation Method of producing microporous polyolefin membrane
US5830554A (en) * 1995-09-26 1998-11-03 Tonen Chemical Corporation Method of producing of microporous polyolefin membrane
US5853633A (en) * 1995-06-19 1998-12-29 Tonen Chemical Corporation Method of producing microporous thermoplastic resin membrane
US5922492A (en) * 1996-06-04 1999-07-13 Tonen Chemical Corporation Microporous polyolefin battery separator
US6057060A (en) * 1994-12-20 2000-05-02 Celgard Inc. Ultra-thin, single-ply battery separator
US6080507A (en) * 1998-04-13 2000-06-27 Celgard Inc. Trilayer battery separator
US6123993A (en) * 1998-09-21 2000-09-26 Advanced Technology Materials, Inc. Method and apparatus for forming low dielectric constant polymeric films
US6180280B1 (en) * 1998-03-12 2001-01-30 Celgard Inc. Trilayer battery separator
US6245272B1 (en) * 1999-02-19 2001-06-12 Tonen Chemical Corporation Polyolefin microporous film and method for preparing the same
US6322923B1 (en) * 1998-01-30 2001-11-27 Celgard Inc. Separator for gel electrolyte battery
US6432586B1 (en) * 2000-04-10 2002-08-13 Celgard Inc. Separator for a high energy rechargeable lithium battery
US6566012B1 (en) * 1999-02-19 2003-05-20 Tonen Chemical Corporation Polyolefin microporous film and method for preparing the same
US6602593B1 (en) * 1999-08-30 2003-08-05 Celgard Inc. Battery separators with reduced splitting propensity
US6666969B1 (en) * 1998-10-01 2003-12-23 Tonen Chemical Corporation Microporous polyolefin film and process for producing the same
US6749961B1 (en) * 2000-04-10 2004-06-15 Celgard Inc. Shutdown battery separator made with a blend of polymer and oligomer
US6824865B1 (en) * 1998-10-01 2004-11-30 Tonen Chemical Corporation Microporous polyolefin film and process for producing the same
US20050014388A1 (en) * 2001-07-27 2005-01-20 Akio Takahashi Polyparaxylylene film, production method therefor and semiconductor device
US20050031941A1 (en) * 2002-11-01 2005-02-10 Celgard Inc. Explosion-proof separator for Li-ion secondary batteries
US6881515B2 (en) * 2001-05-08 2005-04-19 Celgard Inc. Separator for polymer battery
US20050202163A1 (en) * 2004-03-09 2005-09-15 Celgard Inc. Method of making a composite microporous membrane
US20050244717A1 (en) * 2004-04-30 2005-11-03 Celgard Inc. Battery separator with antistatic properties
US20050287425A1 (en) * 2004-06-25 2005-12-29 Celgard Inc. Li/MnO2 battery separators with selective ion transport
US20060046044A1 (en) * 2004-08-24 2006-03-02 Lee Chung J Porous composite polymer dielectric film
US20060088769A1 (en) * 2004-10-22 2006-04-27 Celgard Llc Battery separator with Z-direction stability
US20070072068A1 (en) * 2003-02-21 2007-03-29 Celgard Inc. Oxidation resistant separator for a battery
US20070072069A1 (en) * 2003-11-19 2007-03-29 Tonen Chemical Corporation Microporous composite membrane and its production method and use
US20070221567A1 (en) * 2006-03-22 2007-09-27 Celgard Llc Membrane made of a blend of UHMW polyolefins
US20070238017A1 (en) * 2006-04-07 2007-10-11 Celgard Llc Multilayer separator exhibiting improved strength and stability
US20070264483A1 (en) * 2006-05-15 2007-11-15 Tonen Chemical Corporation Microporous polyolefin membrane, its production method, and battery separator
US20070264578A1 (en) * 2006-05-15 2007-11-15 Tonen Chemical Corporation Microporous polyolefin membrane, its production method and battery separator
US7323207B2 (en) * 2002-10-21 2008-01-29 Philip Morris Usa Inc. Method and apparatus for fingerprint detection
US20080241593A1 (en) * 2006-07-18 2008-10-02 Riken Polyparaxylylene composite film
US20090008816A1 (en) * 2005-03-29 2009-01-08 Tonen Chemical Corporation Method for producing microporous polyolefin membrane and microporous membrane
US20090042008A1 (en) * 2005-11-24 2009-02-12 Tonen Chemical Corporation Microporous polyolefin membrane, its production method, battery separator and battery
US20090079102A1 (en) * 2005-06-24 2009-03-26 Tonen Chemical Corporation Method for producing microporous polyolefin membrane
US20090087749A1 (en) * 2007-09-28 2009-04-02 Tonen Chemical Corporation Microporous Polyolefin Membrane And Manufacturing Method
US20090087750A1 (en) * 2007-09-28 2009-04-02 Tonen Chemical Corporation Microporous Membrane And Manufacturing Method
US20090092893A1 (en) * 2007-10-05 2009-04-09 Tonen Chemical Corporation Microporous Polymer Membrane
US20090098450A1 (en) * 2005-10-24 2009-04-16 Tonen Chemical Corporation Multi-layer, microporous polyolefin membrane, its production method, and battery separator
US20090098341A1 (en) * 2005-03-31 2009-04-16 Tonen Chemical Corporation Microporous polyolefin membrane and method for producing the same
US20090117455A1 (en) * 2005-09-28 2009-05-07 Tonen Chemical Corporation Multi-layer, microporous polyethylene membrane, its production method, and battery separator
US20090117453A1 (en) * 2005-06-24 2009-05-07 Tonen Chemical Corporation Multi-layer, microporous polyethylene membrane, and battery separator and battery using same
US20090127733A1 (en) * 2005-10-21 2009-05-21 Tonen Chemical Corporation Method for producing microporous thermoplastic resin membrane
US20090134538A1 (en) * 2005-10-19 2009-05-28 Tonen Chemical Corporation Method for producing multi-layer, microporous polyolefin membrane
US20090146334A1 (en) * 2005-03-31 2009-06-11 Tonen Chemical Corporation Method for producing microporous polyolefin membrane and microporous membrane
US20090148761A1 (en) * 2005-08-25 2009-06-11 Tonen Chemical Corporation Multi-layer, microporous polyethylene membrane, battery separator formed thereby and battery
US20090170005A1 (en) * 2005-11-01 2009-07-02 Tonen Chemical Corporation Microporous polyolefin membrane, battery separator formed thereby and battery
US20090253032A1 (en) * 2006-04-07 2009-10-08 Tonen Chemical Corporation Multi-layer, microporous polyolefin membrane, its production method, battery separator, and battery
US20090269656A1 (en) * 2005-09-16 2009-10-29 Tonen Chemical Corporation Microporous polyethylene membrane, its production method, and battery separator
US20090269672A1 (en) * 2005-09-28 2009-10-29 Tonen Chemical Corporation Production method of microporous polyethylene membrane and battery separator
US20100003591A1 (en) * 2006-08-01 2010-01-07 Tonen Chemical Corporation Polyolefin composition, its production method, and a battery separator made therefrom
US20110236745A1 (en) * 2008-11-26 2011-09-29 Toray Tonen Specialty Separator Godo Kaisha Microporous membrane, methods for making such film, and the use of such film as battery separator film

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB9026065D0 (en) 1990-11-30 1991-01-16 Chemence Ltd Composition
US6042959A (en) * 1997-10-10 2000-03-28 3M Innovative Properties Company Membrane electrode assembly and method of its manufacture
US20100255376A1 (en) 2009-03-19 2010-10-07 Carbon Micro Battery Corporation Gas phase deposition of battery separators

Patent Citations (77)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3830733A (en) * 1972-03-09 1974-08-20 Union Carbide Corp Diffusion membranes of controlled permeability,apparatus and process
US3940362A (en) * 1972-05-25 1976-02-24 Johnson & Johnson Cross-linked cyanoacrylate adhesive compositions
US5093197A (en) * 1987-12-21 1992-03-03 Entek Manufacturing Inc. Microporous filaments and fibers
US5126219A (en) * 1987-12-21 1992-06-30 Entek Manufacturing Inc. Microporous filaments and fibers, and articles made therefrom
US5230843A (en) * 1987-12-21 1993-07-27 Entek Manufacturing Inc. Process of forming microporous fibers and filaments
US5230949A (en) * 1987-12-21 1993-07-27 Entek Manufacturing Inc. Nonwoven webs of microporous fibers and filaments
US5089360A (en) * 1990-02-08 1992-02-18 Tonen Chemical Corporation High-strength non-woven fabric, method of producing same and battery separator constituted thereby
US5455126A (en) * 1992-07-29 1995-10-03 Martin Marietta Energy Systems, Inc. Electra-optical device including a nitrogen containing electrolyte
US5338625A (en) * 1992-07-29 1994-08-16 Martin Marietta Energy Systems, Inc. Thin film battery and method for making same
US5512147A (en) * 1992-07-29 1996-04-30 Martin Marietta Energy Systems, Inc. Method of making an electrolyte for an electrochemical cell
US5567210A (en) * 1992-07-29 1996-10-22 Martin Marietta Energy Systems, Inc. Method for making an electrochemical cell
US5597660A (en) * 1992-07-29 1997-01-28 Martin Marietta Energy Systems, Inc. Electrolyte for an electrochemical cell
US5332906A (en) * 1992-08-12 1994-07-26 Martin Marietta Energy Systems, Inc. Scintillator assembly for alpha radiation detection and an associated method of making
US5314765A (en) * 1993-10-14 1994-05-24 Martin Marietta Energy Systems, Inc. Protective lithium ion conducting ceramic coating for lithium metal anodes and associate method
US5569520A (en) * 1994-01-12 1996-10-29 Martin Marietta Energy Systems, Inc. Rechargeable lithium battery for use in applications requiring a low to high power output
US5612152A (en) * 1994-01-12 1997-03-18 Martin Marietta Energy Systems, Inc. Rechargeable lithium battery for use in applications requiring a low to high power output
US5561004A (en) * 1994-02-25 1996-10-01 Bates; John B. Packaging material for thin film lithium batteries
US6057060A (en) * 1994-12-20 2000-05-02 Celgard Inc. Ultra-thin, single-ply battery separator
US6132654A (en) * 1994-12-20 2000-10-17 Celgard Inc. Ultra-thin, single-ply battery separator
US5853633A (en) * 1995-06-19 1998-12-29 Tonen Chemical Corporation Method of producing microporous thermoplastic resin membrane
US5830554A (en) * 1995-09-26 1998-11-03 Tonen Chemical Corporation Method of producing of microporous polyolefin membrane
US5922492A (en) * 1996-06-04 1999-07-13 Tonen Chemical Corporation Microporous polyolefin battery separator
US5786396A (en) * 1996-08-21 1998-07-28 Tonen Chemical Corporation Method of producing microporous polyolefin membrane
US6322923B1 (en) * 1998-01-30 2001-11-27 Celgard Inc. Separator for gel electrolyte battery
US6180280B1 (en) * 1998-03-12 2001-01-30 Celgard Inc. Trilayer battery separator
US6080507A (en) * 1998-04-13 2000-06-27 Celgard Inc. Trilayer battery separator
US6123993A (en) * 1998-09-21 2000-09-26 Advanced Technology Materials, Inc. Method and apparatus for forming low dielectric constant polymeric films
US6824865B1 (en) * 1998-10-01 2004-11-30 Tonen Chemical Corporation Microporous polyolefin film and process for producing the same
US6666969B1 (en) * 1998-10-01 2003-12-23 Tonen Chemical Corporation Microporous polyolefin film and process for producing the same
US20090098449A1 (en) * 1998-10-01 2009-04-16 Tonen Chemical Corporation Microporous polyolefin membrane, and method of producing the same
US7479243B2 (en) * 1998-10-01 2009-01-20 Tonen Chemical Corporation Microporous polyolefin membrane, and method of producing the same
US20050058823A1 (en) * 1998-10-01 2005-03-17 Tonen Chemical Corporation Method of producing a microporous polyolefin membrane
US20050098913A1 (en) * 1998-10-01 2005-05-12 Tonen Chemical Corporation Microporous polyolefin membrane, and method of producing the same
US6566012B1 (en) * 1999-02-19 2003-05-20 Tonen Chemical Corporation Polyolefin microporous film and method for preparing the same
US6245272B1 (en) * 1999-02-19 2001-06-12 Tonen Chemical Corporation Polyolefin microporous film and method for preparing the same
US6602593B1 (en) * 1999-08-30 2003-08-05 Celgard Inc. Battery separators with reduced splitting propensity
US6432586B1 (en) * 2000-04-10 2002-08-13 Celgard Inc. Separator for a high energy rechargeable lithium battery
US6749961B1 (en) * 2000-04-10 2004-06-15 Celgard Inc. Shutdown battery separator made with a blend of polymer and oligomer
US6881515B2 (en) * 2001-05-08 2005-04-19 Celgard Inc. Separator for polymer battery
US6946405B2 (en) * 2001-07-27 2005-09-20 Hitachi, Ltd. Polyparaxylylene film, production method therefor and semiconductor device
US20050014388A1 (en) * 2001-07-27 2005-01-20 Akio Takahashi Polyparaxylylene film, production method therefor and semiconductor device
US7323207B2 (en) * 2002-10-21 2008-01-29 Philip Morris Usa Inc. Method and apparatus for fingerprint detection
US20050031941A1 (en) * 2002-11-01 2005-02-10 Celgard Inc. Explosion-proof separator for Li-ion secondary batteries
US20070072068A1 (en) * 2003-02-21 2007-03-29 Celgard Inc. Oxidation resistant separator for a battery
US20070072069A1 (en) * 2003-11-19 2007-03-29 Tonen Chemical Corporation Microporous composite membrane and its production method and use
US20050202163A1 (en) * 2004-03-09 2005-09-15 Celgard Inc. Method of making a composite microporous membrane
US20050244717A1 (en) * 2004-04-30 2005-11-03 Celgard Inc. Battery separator with antistatic properties
US20050287425A1 (en) * 2004-06-25 2005-12-29 Celgard Inc. Li/MnO2 battery separators with selective ion transport
US20060046044A1 (en) * 2004-08-24 2006-03-02 Lee Chung J Porous composite polymer dielectric film
US20060088769A1 (en) * 2004-10-22 2006-04-27 Celgard Llc Battery separator with Z-direction stability
US20090008816A1 (en) * 2005-03-29 2009-01-08 Tonen Chemical Corporation Method for producing microporous polyolefin membrane and microporous membrane
US20090098341A1 (en) * 2005-03-31 2009-04-16 Tonen Chemical Corporation Microporous polyolefin membrane and method for producing the same
US20090146334A1 (en) * 2005-03-31 2009-06-11 Tonen Chemical Corporation Method for producing microporous polyolefin membrane and microporous membrane
US20090117453A1 (en) * 2005-06-24 2009-05-07 Tonen Chemical Corporation Multi-layer, microporous polyethylene membrane, and battery separator and battery using same
US20090079102A1 (en) * 2005-06-24 2009-03-26 Tonen Chemical Corporation Method for producing microporous polyolefin membrane
US20090148761A1 (en) * 2005-08-25 2009-06-11 Tonen Chemical Corporation Multi-layer, microporous polyethylene membrane, battery separator formed thereby and battery
US20090269656A1 (en) * 2005-09-16 2009-10-29 Tonen Chemical Corporation Microporous polyethylene membrane, its production method, and battery separator
US20090269672A1 (en) * 2005-09-28 2009-10-29 Tonen Chemical Corporation Production method of microporous polyethylene membrane and battery separator
US20090117455A1 (en) * 2005-09-28 2009-05-07 Tonen Chemical Corporation Multi-layer, microporous polyethylene membrane, its production method, and battery separator
US20090134538A1 (en) * 2005-10-19 2009-05-28 Tonen Chemical Corporation Method for producing multi-layer, microporous polyolefin membrane
US20090127733A1 (en) * 2005-10-21 2009-05-21 Tonen Chemical Corporation Method for producing microporous thermoplastic resin membrane
US20090098450A1 (en) * 2005-10-24 2009-04-16 Tonen Chemical Corporation Multi-layer, microporous polyolefin membrane, its production method, and battery separator
US20090170005A1 (en) * 2005-11-01 2009-07-02 Tonen Chemical Corporation Microporous polyolefin membrane, battery separator formed thereby and battery
US20090042008A1 (en) * 2005-11-24 2009-02-12 Tonen Chemical Corporation Microporous polyolefin membrane, its production method, battery separator and battery
US20070221567A1 (en) * 2006-03-22 2007-09-27 Celgard Llc Membrane made of a blend of UHMW polyolefins
US20070238017A1 (en) * 2006-04-07 2007-10-11 Celgard Llc Multilayer separator exhibiting improved strength and stability
US20090253032A1 (en) * 2006-04-07 2009-10-08 Tonen Chemical Corporation Multi-layer, microporous polyolefin membrane, its production method, battery separator, and battery
US20090286161A1 (en) * 2006-04-07 2009-11-19 Tonen Chemical Corporation Microporous polyolefin membrane, its production method, battery separator, and battery
US20100021808A1 (en) * 2006-04-07 2010-01-28 Tonen Chemical Corporation Multi-layer, microporous polyolefin membrane, its production method, battery separator, and battery
US20070264578A1 (en) * 2006-05-15 2007-11-15 Tonen Chemical Corporation Microporous polyolefin membrane, its production method and battery separator
US20070264483A1 (en) * 2006-05-15 2007-11-15 Tonen Chemical Corporation Microporous polyolefin membrane, its production method, and battery separator
US20080241593A1 (en) * 2006-07-18 2008-10-02 Riken Polyparaxylylene composite film
US20100003591A1 (en) * 2006-08-01 2010-01-07 Tonen Chemical Corporation Polyolefin composition, its production method, and a battery separator made therefrom
US20090087750A1 (en) * 2007-09-28 2009-04-02 Tonen Chemical Corporation Microporous Membrane And Manufacturing Method
US20090087749A1 (en) * 2007-09-28 2009-04-02 Tonen Chemical Corporation Microporous Polyolefin Membrane And Manufacturing Method
US20090092893A1 (en) * 2007-10-05 2009-04-09 Tonen Chemical Corporation Microporous Polymer Membrane
US20110236745A1 (en) * 2008-11-26 2011-09-29 Toray Tonen Specialty Separator Godo Kaisha Microporous membrane, methods for making such film, and the use of such film as battery separator film

Cited By (71)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8603683B2 (en) 2009-03-19 2013-12-10 Enevate Corporation Gas phase deposition of battery separators
US9647259B2 (en) 2009-03-19 2017-05-09 Enevate Corporation Gas phase deposition of battery separators
US11769870B2 (en) 2009-07-16 2023-09-26 Enevate Corporation Carbon electrode structures for batteries
US11515528B2 (en) 2009-09-29 2022-11-29 Georgia Tech Research Corporation Electrodes, lithium-ion batteries, and methods of making and using same
US11522176B2 (en) 2009-09-29 2022-12-06 Georgia Tech Research Corporation Electrodes, lithium-ion batteries, and methods of making and using same
US11557757B2 (en) 2009-09-29 2023-01-17 Sila Nanotechnologies, Inc. Electrodes, lithium-ion batteries, and methods of making and using same
US11715825B2 (en) 2009-09-29 2023-08-01 Georgia Tech Research Corporation Electrodes, lithium-ion batteries, and methods of making and using same
US10461366B1 (en) 2010-01-18 2019-10-29 Enevate Corporation Electrolyte compositions for batteries
US11183712B2 (en) 2010-01-18 2021-11-23 Enevate Corporation Electrolyte compositions for batteries
US11728476B2 (en) 2010-01-18 2023-08-15 Enevate Corporation Surface modification of silicon particles for electrochemical storage
US11196037B2 (en) 2010-01-18 2021-12-07 Enevate Corporation Silicon particles for battery electrodes
US11955623B2 (en) 2010-01-18 2024-04-09 Enevate Corporation Silicon particles for battery electrodes
US10622620B2 (en) 2010-01-18 2020-04-14 Enevate Corporation Methods of forming composite material films
US11380890B2 (en) 2010-01-18 2022-07-05 Enevate Corporation Surface modification of silicon particles for electrochemical storage
US9997765B2 (en) 2010-12-22 2018-06-12 Enevate Corporation Electrodes, electrochemical cells, and methods of forming electrodes and electrochemical cells
US10431808B2 (en) 2010-12-22 2019-10-01 Enevate Corporation Electrodes, electrochemical cells, and methods of forming electrodes and electrochemical cells
US10985361B2 (en) 2010-12-22 2021-04-20 Enevate Corporation Electrodes configured to reduce occurrences of short circuits and/or lithium plating in batteries
US11837710B2 (en) 2010-12-22 2023-12-05 Enevate Corporation Methods of reducing occurrences of short circuits and/or lithium plating in batteries
US11784298B2 (en) 2010-12-22 2023-10-10 Enevate Corporation Methods of reducing occurrences of short circuits and/or lithium plating in batteries
US10516155B2 (en) 2010-12-22 2019-12-24 Enevate Corporation Electrodes, electrochemical cells, and methods of forming electrodes and electrochemical cells
US11177467B2 (en) 2010-12-22 2021-11-16 Enevate Corporation Electrodes, electrochemical cells, and methods of forming electrodes and electrochemical cells
US10388943B2 (en) 2010-12-22 2019-08-20 Enevate Corporation Methods of reducing occurrences of short circuits and/or lithium plating in batteries
JP2012144588A (en) * 2011-01-07 2012-08-02 Univ Of Tokyo Porous membrane, porous structure, method for producing those and sensor
US10603867B1 (en) 2011-05-24 2020-03-31 Enevate Corporation Carbon fibers and methods of producing the same
US11411212B2 (en) 2012-08-24 2022-08-09 Sila Nanotechnologies, Inc. Scaffolding matrix with internal nanoparticles
US11942624B2 (en) 2012-08-24 2024-03-26 Sila Nanotechnologies, Inc. Scaffolding matrix with internal nanoparticles
US11374215B2 (en) 2012-08-24 2022-06-28 Sila Nanotechnologies, Inc. Scaffolding matrix with internal nanoparticles
US10680274B2 (en) 2013-03-14 2020-06-09 Enevate Corporation Clamping device for an electrochemical cell stack
US10985397B2 (en) 2013-03-14 2021-04-20 Enevate Corporation Clamping device for an electrochemical cell stack
CN106159159A (en) * 2015-05-14 2016-11-23 Sk新技术株式会社 Secondary cell composite separating film and preparation method thereof
US10403902B2 (en) 2015-05-15 2019-09-03 Composite Materials Technology, Inc. High capacity rechargeable batteries
US10541412B2 (en) 2015-08-07 2020-01-21 Enevate Corporation Surface modification of silicon particles for electrochemical storage
US11171375B2 (en) 2016-03-25 2021-11-09 Enevate Corporation Stepped electrochemical cells with folded sealed portion
USRE49419E1 (en) 2016-09-01 2023-02-14 Composite Materials Technology, Inc. Nano-scale/nanostructured Si coating on valve metal substrate for lib anodes
US20180342734A1 (en) * 2017-05-15 2018-11-29 Millibatt, Inc. Electrolyte material, battery assembly, and production method
US10615417B2 (en) * 2017-05-15 2020-04-07 Millibatt, Inc. Electrolyte material, battery assembly, and production method
US11309580B2 (en) 2017-12-07 2022-04-19 Enevate Corporation Methods of forming electrochemical cells
US11075408B2 (en) 2017-12-07 2021-07-27 Enevate Corporation Silicon-based energy storage devices with fluorinated polymer containing electrolyte additives
US11309536B2 (en) 2017-12-07 2022-04-19 Enevate Corporation Silicon particles for battery electrodes
US11283069B2 (en) 2017-12-07 2022-03-22 Enevate Corporation Silicon-based energy storage devices with fluorinated cyclic compound containing electrolyte additives
US10686214B2 (en) 2017-12-07 2020-06-16 Enevate Corporation Sandwich electrodes and methods of making the same
US10707478B2 (en) 2017-12-07 2020-07-07 Enevate Corporation Silicon particles for battery electrodes
US11923506B2 (en) 2017-12-07 2024-03-05 Enevate Corporation Silicon-based energy storage devices with ether containing electrolyte additives
US11411249B2 (en) 2017-12-07 2022-08-09 Enevate Corporation Silicon-based energy storage devices with cyclic carbonate containing electrolyte additives
US11916228B2 (en) 2017-12-07 2024-02-27 Enevate Corporation Binding agents for electrochemically active materials and methods of forming the same
US11456484B2 (en) 2017-12-07 2022-09-27 Enevate Corporation Silicon-based energy storage devices with linear carbonate containing electrolyte additives
US11908992B2 (en) 2017-12-07 2024-02-20 Enevate Corporation Methods of forming electrochemical cells
US11901500B2 (en) 2017-12-07 2024-02-13 Enevate Corporation Sandwich electrodes
US11888114B2 (en) 2017-12-07 2024-01-30 Enevate Corporation Silicon-based energy storage devices with fluorinated polymer containing electrolyte additives
US10763538B2 (en) 2017-12-07 2020-09-01 Enevate Corporation Methods of forming electrochemical cells
US11539041B2 (en) 2017-12-07 2022-12-27 Enevate Corporation Silicon particles for battery electrodes
US10811727B2 (en) 2017-12-07 2020-10-20 Enevate Corporation Silicon-based energy storage devices with ether containing electrolyte additives
US11133498B2 (en) 2017-12-07 2021-09-28 Enevate Corporation Binding agents for electrochemically active materials and methods of forming the same
US11349153B2 (en) 2017-12-07 2022-05-31 Enevate Corporation Silicon-based energy storage devices with ether containing electrolyte additives
US10978739B2 (en) 2017-12-07 2021-04-13 Enevate Corporation Silicon-based energy storage devices with carboxylic ether, carboxylic acid based salt, or acrylate electrolyte containing electrolyte additives
US11777077B2 (en) 2017-12-07 2023-10-03 Enevate Corporation Silicon particles for battery electrodes
US10847792B2 (en) 2017-12-07 2020-11-24 Enevate Corporation Prelithiated and methods for prelithiating an energy storage device
US11819806B1 (en) * 2018-10-15 2023-11-21 Ampcera Inc. Methods for manufacturing a solid state ionic conductive membrane on a macro porous support scaffold
US10957898B2 (en) 2018-12-21 2021-03-23 Enevate Corporation Silicon-based energy storage devices with anhydride containing electrolyte additives
US11165099B2 (en) 2018-12-21 2021-11-02 Enevate Corporation Silicon-based energy storage devices with cyclic organosilicon containing electrolyte additives
US11837711B2 (en) 2018-12-21 2023-12-05 Enevate Corporation Silicon-based energy storage devices with anhydride containing electrolyte additives
US11398641B2 (en) 2019-06-05 2022-07-26 Enevate Corporation Silicon-based energy storage devices with silicon containing electrolyte additives
WO2021221673A1 (en) * 2020-04-30 2021-11-04 Hzo, Inc. Plasma assisted parylene deposition
US20220336932A1 (en) * 2020-08-19 2022-10-20 Millibatt, Inc. Three-dimensional folded battery unit and methods for manufacturing the same
US11476549B2 (en) 2020-08-19 2022-10-18 Millibatt, Inc. Three-dimensional folded battery unit and methods for manufacturing the same
US11411289B2 (en) 2020-08-19 2022-08-09 Millibatt, Inc. Three-dimensional folded battery unit and methods for manufacturing the same
US11923563B2 (en) * 2020-08-19 2024-03-05 Millibatt, Inc. Three-dimensional folded battery unit and methods for manufacturing the same
US11936071B2 (en) * 2020-08-19 2024-03-19 Millibatt, Inc. Three-dimensional folded battery unit and methods for manufacturing the same
US20230006316A1 (en) * 2020-08-19 2023-01-05 Millibatt, Inc. Three-dimensional folded battery unit and methods for manufacturing the same
US11387443B1 (en) 2021-11-22 2022-07-12 Enevate Corporation Silicon based lithium ion battery and improved cycle life of same
CN114204133A (en) * 2021-12-09 2022-03-18 惠州亿纬锂能股份有限公司 Method for solving expansion of winding type battery cell

Also Published As

Publication number Publication date
US9647259B2 (en) 2017-05-09
US20130130120A1 (en) 2013-05-23
US20140065322A1 (en) 2014-03-06
US8603683B2 (en) 2013-12-10

Similar Documents

Publication Publication Date Title
US9647259B2 (en) Gas phase deposition of battery separators
Kim et al. Plasma-modified polyethylene membrane as a separator for lithium-ion polymer battery
JP5408702B2 (en) Lithium ion battery
JP4477856B2 (en) Separator having inorganic protective film and lithium battery employing the same
KR100906251B1 (en) Gel-typed Polymer Electrolyte Containing Diacryl Amide-based Polymeric Material and Electrochemical Device Comprising the Same
JP7414709B2 (en) LI ion battery without olefin separator
KR101614885B1 (en) Protection layer for lithium electrode for lithium secondary battery and lithium secondary battery using the same
US10756320B2 (en) Method for making a lithium-sulfur battery separator
KR20140112597A (en) Lithium metal electrode modified by conductive polymer, method for preparing the same and lithium metal battery comprising the same
KR102593601B1 (en) Method of preparing lithium secondary battery thick-film and lithium secondary battery using electro-slurry-spraying of slurry including sulfide-based solid electrolyte
CA3148530A1 (en) Structured anodes for lithium-based energy storage devices
US20210057755A1 (en) Anodes for lithium-based energy storage devices
KR20140147412A (en) Case for electrochemical device containing volume expansibile material and electrochemical device comprising the same
JP2016537784A (en) Copolymers for bipolar batteries
JP5187720B2 (en) Lithium ion polymer battery
US10756381B2 (en) Lithium-sulfur battery separator and lithium-sulfur battery using the same
JPWO2019188719A1 (en) Manufacturing method of laminate for non-aqueous secondary battery and manufacturing method of non-aqueous secondary battery
Aravindan et al. Comparison among the performance of LiBOB, LiDFOB and LiFAP impregnated polyvinylidenefluoride-hexafluoropropylene nanocomposite membranes by phase inversion for lithium batteries
TW201529653A (en) Porous separator having inverse opal structure for secondary battery and method for manufacturing the same
KR101861996B1 (en) Metal electrode with patterned surface morphology for batteries and Its Preparation Method
KR20220055930A (en) Coating composition for separator of secondary battery and method of manufacturing the same
CN114342148A (en) Method for manufacturing secondary battery
JP4197804B2 (en) Method for manufacturing lithium secondary battery
CN115004405B (en) Method for manufacturing secondary battery
KR101057351B1 (en) Gel polymer electrolyte application device

Legal Events

Date Code Title Description
AS Assignment

Owner name: CARBON MICRO BATTERY CORPORATION, CALIFORNIA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:PARK, BENJAMIN;GORKOVENKO, ALEXANDER;ZAOUK, RABIH;AND OTHERS;SIGNING DATES FROM 20100514 TO 20100602;REEL/FRAME:024570/0692

AS Assignment

Owner name: ENOVATE CORPORATION, CALIFORNIA

Free format text: CHANGE OF NAME;ASSIGNOR:CARBON MICRO BATTERY CORPORATION;REEL/FRAME:025650/0450

Effective date: 20100712

AS Assignment

Owner name: ENEVATE CORPORATION, CALIFORNIA

Free format text: CHANGE OF NAME;ASSIGNOR:ENOVATE CORPORATION;REEL/FRAME:025665/0732

Effective date: 20100903

STCB Information on status: application discontinuation

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