Classifications

• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
  • H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
  • H01G11/22—Electrodes
  • H01G11/26—Electrodes characterised by their structure, e.g. multi-layered, porosity or surface features
  • H01G11/28—Electrodes characterised by their structure, e.g. multi-layered, porosity or surface features arranged or disposed on a current collector; Layers or phases between electrodes and current collectors, e.g. adhesives
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
  • H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
  • H01G11/54—Electrolytes
  • H01G11/58—Liquid electrolytes
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
  • H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
  • H01G11/66—Current collectors
  • H01G11/68—Current collectors characterised by their material
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
  • H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
  • H01G11/66—Current collectors
  • H01G11/70—Current collectors characterised by their structure
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
  • H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
  • H01G11/84—Processes for the manufacture of hybrid or EDL capacitors, or components thereof
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/02—Electrodes composed of, or comprising, active material
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
  • H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
  • H01G11/22—Electrodes
  • H01G11/30—Electrodes characterised by their material
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
  • H01G9/00—Electrolytic capacitors, rectifiers, detectors, switching devices, light-sensitive or temperature-sensitive devices; Processes of their manufacture
  • H01G9/004—Details
  • H01G9/04—Electrodes or formation of dielectric layers thereon
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
  • H01G9/00—Electrolytic capacitors, rectifiers, detectors, switching devices, light-sensitive or temperature-sensitive devices; Processes of their manufacture
  • H01G9/145—Liquid electrolytic capacitors
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
  • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
  • Y02E60/13—Energy storage using capacitors

Definitions

• the present invention relates to current-collector conductive electrodes in particular used in energy storage systems such as supercapacitors. More specifically, the present invention relates to a conductive electrode comprising a current collector comprising at least one protective conductive layer and the method of manufacturing said current collector.
• Supercapacitors are electrical energy storage systems of particular interest for applications requiring the conveyance of high power electrical energy.
• the ability to charge and discharge fast, the longer life compared to a high power battery make supercapacitors promising candidates for many applications.
• Supercapacitors generally consist of the combination of two conductive electrodes with a high specific surface area, immersed in an ionic electrolyte and separated by an insulating membrane called "separator", which allows ionic conductivity and avoids electrical contact between the electrodes.
• Each electrode is in contact with a metal current collector for the exchange of electric current with an external system.
• the ions present in an electrolyte are attracted by the surface having an opposite charge thus forming a double electrochemical layer at the interface of each electrode. The electrical energy is thus stored electrostatically by separating the charges.
• e the thickness of the double layer.
• the carbon electrodes used in supercapacitive systems must necessarily be:
• the energy stored in the supercapacitor is defined according to the conventional expression of the capacitors, namely:
• capacity and potential are two essential parameters that must be optimized to promote energy performance.
• the potential depends mainly on the nature of the electrolyte.
• electrolytes There are typically different types of electrolytes.
• a family is the family of organic electrolytes, that is to say comprising an organic salt dispersed in an organic solvent. Some of these electrolytes allow to reach a potential of operation of 2.7V.
• these electrolytes are expensive, flammable, toxic and potentially polluting. They thus pose security problems for use in a vehicle.
• Aqueous electrolytes are inexpensive and non-flammable, so they are more interesting for this application.
• aqueous medium the applicable potential is 1.2V.
• Various aqueous electrolytes may be used, for example an aqueous solution of sulfuric acid, or potassium chloride, or potassium sulfate, or other salts in acidic, basic or neutral medium.
• the capacity depends on the porous texture actually accessible by the electrolyte, the potential depends directly on the stability of the electrolyte under the influence of the electric field.
• a known solution is to add active material to the supercapacitors. There are different possibilities for incorporating the active ingredient into a supercapacitor.
• PCT / FR2009 / 000332 describes the use of monolithic carbons in supercapacitors having high mass capacities. To achieve high energy densities, it is therefore particularly interesting to incorporate the active ingredient in the system as a monolith. Indeed, in this case, no inert binder is needed to disperse the active ingredient, which allows ipso facto to increase the achievable energy density.
• the resistance to current flow in the system must be very low. Indeed, this resistance generates losses by Joule effect, which reduce the efficiency of the supercapacitor.
• This resistance is the sum of the resistances of the various components of the system, and in particular the resistance of the electrolyte, and the resistance of the current collectors.
• a primary contribution is the resistance of the interface between the current collector and the active ingredient. This resistance is dependent on the quality and nature of the contact.
• it is necessary to use metals of high conductivities In addition for the sake of economy and ease of use, the metals used must be inexpensive and can be shaped easily.
• metals that can be favorably used are therefore typically copper and aluminum.
• the use of these materials in an aqueous medium poses problems of chemical and electrochemical stability. Indeed, at a typical oxidation potential in an aqueous medium of 1.2V, most metals corrode.
• EP1032064 discloses a current collector of a positive electrode consisting of a paste of active material comprising a polymer layer comprising an oxalate and a compound based on silicon, phosphate or chromium. This solution makes it possible to protect the collector during the removal of the paste of active material but has no effect on the characteristics of the electrode in use. Moreover, this strategy can not be used in the case of a monolith as an active ingredient. It is therefore necessary to use an interface between the metal current collector and the monolithic active material.
• Document FR2824418 describes a current collector coated with a paint layer comprising conductive particles, such as graphite or carbon black.
• the paint is applied between the collector and the active ingredient and is then heated to remove the solvent.
• the paint is epoxy base or polyurethane base.
• This layer of paint protects the collector in an organic medium, but no information is given on its effectiveness to protect the collector of an aqueous electrolyte.
• these paints are crosslinked, therefore little deformable and can not thus conform to the surface of the active material when it is present in the form of monolith, which increases the contact resistance and thus prevents optimal operation of the supercapacitor.
• WO2007 / 036641 discloses a method of depositing a carbon thin film by depositing a dispersion of carbonaceous particles in a sol-gel polymer followed by the removal of said sol-gel polymer at high temperature. This additional layer makes it possible to improve the conduction properties at the contact. Nevertheless, no information is given on its watertightness in an aqueous medium. In addition, the carbon films obtained by this method are fragile and subject to abrasion during assembly of the electrodes.
• One of the aims of the invention is therefore to provide a current collector and its manufacturing method, having properties of optimized durability and conductivity, especially in its use within a monolithic active material electrode.
• the present invention relates to a conductive electrode for an aqueous electrolyte solution electrical energy storage system, said electrode comprising a current collector. metal and an active material, said metal current collector having a protective conductive layer placed between said current collector and said active material, said protective conductive layer comprising:
• the metal current collector comprises at least one additional protective conductive layer placed on the protective conductive layer.
• the protective conductive layer comprises:
• the copolymer comprises units of vinyl chloride and / or vinyl acetate and / or carboxylic acid groups.
• the copolymer matrix further comprises additives.
• the conductive fillers are chosen from carbon black and / or graphite and / or carbon nanotubes.
• the thickness of the protective conductive layer is between 5 and 50 micrometers.
• the active ingredient is a monolithic active material.
• the monolithic active material is a carbon monolith.
• the present invention also relates to a method of manufacturing a metal current collector for an electrical energy storage system, said metal current collector being intended to come into electrical contact with an active material to form a conductive electrode with a solution of aqueous electrolyte, and comprising a protective conductive layer, comprising the following steps:
• composition comprising 30% to 85% of a copolymer in proportion by weight of dry matter and 70% to 15% of conductive fillers in proportion by weight of dry matter, in addition to the proportion by weight of dry matter of a copolymer in order to reach a total of 100%, diluted in a solvent in order to reach a viscosity of 1000 mPa to 10000 mPa at 50 rpm,
• the latter further comprises, following the second heat treatment step, the following steps of applying at least one additional protective conductive layer:
• composition comprising 30% to 85% of a copolymer in proportion by weight of dry matter and 70% to 15% of conductive fillers in proportion by weight of dry matter, in addition to the proportion by weight of dry matter of a copolymer in order to reach a total of 100%, diluted in a solvent in order to reach a viscosity of 1000 mPa to 10000 mPa at 50 rpm,
• the final viscosity of the composition is 7200mPa at 50rpm.
• the composition comprises 50% to 65% of copolymer in proportion by weight of dry matter, 50% to 35% of conductive fillers in proportion by weight of dry matter, in addition to the proportion by weight of copolymer solids in order to reach a total of 100%.
• the copolymer comprises units of vinyl chloride and / or vinyl acetate and / or carboxylic acid groups.
• the composition comprising 30% to 85% of a copolymer in proportion by weight of dry matter and 70% to 15% of conductive fillers in proportion by weight of dry matter, further comprises additives ..
• the conductive fillers are chosen from carbon black and / or graphite and / or carbon nanotubes.
• the step of depositing the composition on the metal current collector is carried out using a film puller.
• the first and second heat treatment steps have a duration of 30 minutes each.
• FIG. 1 shows a schematic representation of the structure of a supercapacitor
• FIG. 2 shows a schematic representation of a test structure carried out for the measurement of the contact resistances
• FIG. 3 shows a graph of the results of electrochemical impedance spectroscopy measurements of an example according to the invention.
• Figure 1 shows a schematic representation of the structure of a supercapacitor 1.
• the supercapacitor 1 comprises two conductive electrodes immersed in an ionic electrolyte (not shown) and separated by an insulating membrane called separator 9, which allows the ionic conductivity and avoids electrical contact between the electrodes.
• Each electrode comprises a metal current collector 3, for example copper or aluminum, covered with a protective conductive layer 5, for example with a thickness of between 5 and 50 microns, and a monolithic active material 7, for example. carbon example, in contact with the separator 9.
• the protective layer 5 is watertight to aqueous electrolytes, especially in acidic medium, for example at a pH of less than or equal to 4, or in neutral medium at a pH of 7. This sealing thus allows a protection of the metal current collector 3 against corrosion in aqueous media, thus preventing a deterioration of the electrical contact between said metal current collector 3 and the monolithic active material 7 .
• the protective conductive layer 5 also makes it possible to improve the electrical contact between said metal current collector 3 and the monolithic active material 7.
• the protective conductive layer 5 preferably comprises between 30% and 85% by weight proportion of material drying of a copolymer matrix and between 70% and 15% by weight of dry matter of conductive fillers, in addition to the proportion by weight of copolymer solids to reach a total of 100%.
• a copolymer makes it possible to improve the flexibility of a protective conductive layer 5, which is favorable for reducing the contact resistance.
• a copolymer adheres more easily to a metal surface which avoids the use of additives capable of migrating into the electrolyte during use of the electrode and to disrupt its operation.
• the copolymer used preferably comprises vinyl chloride and / or vinyl acetate units and / or carboxylic acid groups, for example Vinnol H15 / 45 M.
• the copolymer matrix may further comprise additives such as crosslinking agents, wetting agents, dispersants or stabilizers.
• the conductive fillers are preferably chosen from carbon black and / or graphite and / or carbon nanotubes.
• the metal current collector 3 may comprise at least one additional protective conductive layer (not shown) placed on the protective conductive layer 5.
• the at least one additional protective conductive layer may be similar to the conductive protective layer 5 and therefore have characteristics similar to the latter.
• the addition of at least one additional protective conductive layer on the protective layer 5 makes it possible to increase the protection of the metal current collector 3.
• the method of manufacturing the metal current collector 3, covered with the conductive layer protection 5 is done in several steps.
• the first step is a step of preparing a composition comprising 30% to 85% of a copolymer in proportion by weight of dry matter and in addition 70% to 15% of conductive fillers in proportion by weight of dry matter, in addition the proportion by weight of copolymer solids to reach a total of 100%.
• the copolymer used preferably comprises vinyl chloride units and / or vinyl acetate and / or carboxylic acid groups, such as Vinnol H15 / 45 M.
• the conductive fillers are preferably chosen from carbon black and / or graphite and / or carbon nanotubes.
• This composition is diluted in a solvent, for example methyl isobutyl ketone (MIBK), in order to reach a viscosity value of between 1000 mPa and 100 100 mPa, measured with a Brookfield viscometer.
• MIBK methyl isobutyl ketone
• composition may further comprise additives such as crosslinking agents, wetting agents, dispersants or stabilizers.
• the second step is a layer application step of the composition on the metal current collector 3, for example by means of a film puller.
• the third step is a heat treatment step of the metal current collector 3 covered, at a temperature below the boiling point of the solvent, but sufficient in order to have evaporation and thus a disappearance of a large part of the solvent. the composition.
• This heat treatment step thus removes the solvent from the protective conductive layer 5 covering the metal current collector 3, while retaining the mechanical properties of the latter.
• the fourth step is again a heat treatment step of the metal current collector 3 covered.
• This new heat treatment is performed at a temperature above the glass transition temperature (tg) of the copolymer and at the boiling point of the solvent, said heat treatment temperature being however lower than the degradation temperature of the copolymer.
• degradation temperature is meant the temperature at which the copolymer is destroyed and disappears from the protective conductive layer 5.
• the glass transition temperature (tg) of the copolymer may for example be 75 ° C. for Vinnol H15 / 45 M, measured by differential scanning calorimetry (DSC) with a rate of rise of 10 ° C. per minute.
• This second heat treatment makes it possible to eliminate the excess of solvent as well as to reinforce the tightness of the protective conductive layer 5.
• the duration of each heat treatment of the third and fourth stages may for example be 30 minutes in order to be optimal.
• the manufacturing method further comprises additional steps of applying said additional protective conductive layer. These steps are performed following the second heat treatment step and are as follows:
• composition comprising 30% to 85% of a copolymer in proportion by weight of dry matter and 70% to 15% of conductive fillers in proportion by weight of dry matter, in addition to the proportion by weight of dry matter of copolymer in order to reach a total of 100%, diluted in a solvent in order to reach a viscosity of 1000 mPa to 1000 mPa at 50 rpm, for example by means of a film puller,
• compositions having a final viscosity of 7200mPa at 50rpm used to manufacture a metal current collector 3 covered with a protective conductive layer 5 according to the invention.
• compositions used in these examples all comprise between 50% and 65% by weight of dry matter of a copolymer matrix and in addition between 50% and 35% by weight of dry matter of conductive fillers, in addition to the proportion by weight of copolymer solids to reach a total of 100%.
• Table 1 Examples of composition formulation.
• a measurement of the electrical resistance is performed on a test structure illustrated in FIG.
• a 100 micron thick layer of these compositions is deposited on a copper current collector 3 using a film puller for homogeneous and controlled removal.
• the covered copper current collector 3 is then treated at 120 ° C. for 30 minutes.
• the thickness of the protective conductive layer 5 is measured using a micrometer, and is between 20 and 30 micrometers for each face.
• the test structure illustrated in FIG. 2 then comprises a monolithic carbon 3 2.5 * 2.5 cm in area and 0.7 mm thick placed between two covered copper current collectors 3 and pressurized with a weight 11, by example 200N, which allows to characterize the electrical contacts.
• the measured resistance should be as low as possible to allow high power operation of the supercapacitor
• a protective conductive layer 5 is deposited on glass according to the same method previously used, in order to measure the conductivity of said protective conductive layer 5. This measurement is performed by a four-point conductivity test. classic.
• the sealing of the protective conductive layer 5 is characterized by electrochemical impedance spectroscopy (EIS) of model cells operating at a voltage of IV, before and after 1000 galvanostatic cycles at 0.125 A / g.
• EIS electrochemical impedance spectroscopy
• model cells identical to the structure of a supercapacitor 1 represented by FIG. 1, are obtained by assembling two monolithic carbons 7 of 0.7 mm thickness on two coated copper current collectors 3 between which a separator 5 is placed. The assembly is filled with electrolyte diluted in water and packaged between two plastic films. A first test series is carried out in an acidic medium with a 1M sulfuric acid (H 2 SO 4 ) electrolyte and a second test series is carried out in a neutral medium with a 5M sodium perchlorate (NaClO) electrolyte.
• H 2 SO 4 1M sulfuric acid
• NaClO sodium perchlorate
• the EIS makes it possible to highlight the existence of parasitic faradic phenomena. These reactions occur when the copper is exposed to the electrolyte. In this case, during the cycling, the metal is degraded, and the device can no longer function.
• the protective conductive layer 5 obtained with the composition of Example 4 of Example 4 was then scratched using a scalpel blade to leave the apparent copper.
• the behavior observed shows faradic phenomena related to the oxidation of copper, the leak test is considered to have failed.
• the protective conductive layer 5 described in Examples 1 to 5 not only makes it possible to protect the metal collector from the degradation associated with the oxidation in the presence of electrolyte, but also surprisingly improve the electrical contact between the collector and the monolithic active material with respect to an uncoated collector.

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• Engineering & Computer Science (AREA)
• Power Engineering (AREA)
• Microelectronics & Electronic Packaging (AREA)
• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Electrochemistry (AREA)
• Materials Engineering (AREA)
• Manufacturing & Machinery (AREA)
• General Chemical & Material Sciences (AREA)
• Electric Double-Layer Capacitors Or The Like (AREA)
• Cell Electrode Carriers And Collectors (AREA)
• Battery Electrode And Active Subsutance (AREA)

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• 2011
  • 2011-07-01 FR FR1102075A patent/FR2977364B1/fr not_active Expired - Fee Related
• 2012
  • 2012-07-02 EP EP12730981.3A patent/EP2727122A1/fr not_active Withdrawn
  • 2012-07-02 KR KR1020147002537A patent/KR20140057251A/ko not_active Application Discontinuation
  • 2012-07-02 CN CN201280041334.2A patent/CN103748648B/zh not_active Expired - Fee Related
  • 2012-07-02 RU RU2014103453/07A patent/RU2600566C2/ru not_active IP Right Cessation
  • 2012-07-02 WO PCT/EP2012/062848 patent/WO2013004666A1/fr active Application Filing
  • 2012-07-02 US US14/130,159 patent/US9384907B2/en not_active Expired - Fee Related
  • 2012-07-02 CA CA2840276A patent/CA2840276A1/en not_active Abandoned
  • 2012-07-02 JP JP2014517760A patent/JP2014523121A/ja active Pending
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  • 2012-07-02 MX MX2013015432A patent/MX347023B/es active IP Right Grant
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