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    • 专利摘要:
    Electrodes for rechargeable lithium batteries. The present invention relates to a ceramic electrode active with lithium, absent of polymeric binders and with thicknesses greater than 50 μm, its manufacturing process, and its use in rechargeable batteries. (Machine-translation by Google Translate, not legally binding)
    公开号:ES2633149A1
    申请号:ES201630313
    申请日:2016-03-16
    公开日:2017-09-19
    发明作者:José Manuel Amarilla Álvarez；Belén LEVENFELD LAREDO；Mª Eugenia SOTOMAYOR LOZANO；Alejandro VÁREZ ÁLVAREZ；Jean Yves SÁNCHEZ；Wilmer BUCHELI ERAZO
    申请人:Consejo Superior de Investigaciones Cientificas CSIC；Universidad Carlos III de Madrid；
    IPC主号:
    专利说明:

    ELECTRODES FOR LITHIUM RECHARGEABLE BATTERIES DESCRIPTION

    The present invention relates to an electrode of lithium active ceramic material, absent from polymeric binders and with thicknesses greater than 50 µm, its manufacturing process, and its use in rechargeable batteries.
    STATE OF THE TECHNIQUE
     10
    Li-ion batteries are the most advanced technology in commercial rechargeable batteries. However, the strong demands for electrical energy requested by new applications, such as portable electronic equipment, electric cars or the large storage systems required by renewable energy, make it necessary to develop new rechargeable batteries capable of storing more energy.

    At present, the electrodes used in conventional Li-ion batteries are manufactured by calendering techniques of an active material powder paste, binders (binders), solvents and additives, which extend and deposit in metal sheets that act as current collectors (aluminum for the cathode and copper for the anode). The presence of these binders, solvents and additives are those that generally limit the working temperature range and are also, in some cases, the causes of explosions and combustion of commercial lithium-ion batteries. 25

    On the other hand, powder extrusion molding is a process derived from the powder injection molding process and has been used for the manufacture of hard metal bars and refractory metals (JC Zhou JC et al., J. Mat. Proc. Techn., 2003, 137 (1-2), 21-24; Liu, WS et al. Rare Metals Mat. & Eng., 2012, 41 (8), 1495-1499). 30 However, it has not been used to date for the manufacture of ceramic sheets with applications in rechargeable lithium batteries.

    Both extrusion molding and powder injection techniques have the ability to produce, at comparatively low costs, components of complex geometry (especially in the case of injection) and with high precision. Subjects
    used premiums usually contain 70% by volume of ceramic powders, and 30% of additives such as waxes, lubricants and plasticizers, which make up the binder system; and the process consists of four main stages: mixing, molding, binder removal and sintering.
     5
    The process of removing the binder from the shaped piece must be progressive from the outside to the inside of it. And, therefore, the thickness of the piece hinders the process of removing additives.

    The technology of extrusion molding of powders is a manufacturing method 10 of sheets more effective for ceramic pieces than the uniaxial pressing, whose main limitation is the thicknesses obtained in large parts.

    Given this background, the well-known powder extrusion technology (Jardiel, T. et al. Ceramics International, 2009, 35 (6), 2329-2335; Monzón, H. et 15 al. International Journal of Hydrogen Energy, 2014, 39 (10), 5470-5476) is presented in this patent as an effective method for the manufacture of ceramic electrodes (anodes and cathodes) with application in rechargeable lithium batteries, allowing to have sheets formed solely by the active material of electrode and therefore, free of additives, which gives it a high added value, since the electrodes 20 of commercial rechargeable batteries are composite materials (composites) formed by the active material and a variable number of additives that improve their electrical properties and mechanical

    These additives, being electrochemically inactive materials, entail increasing the weight of the battery without increasing the capacity or specific energy of the active material. In addition, its use entails a limitation in terms of the operating temperature range of the battery, which may lead to safety problems when operating at high temperature.
     30
    Particularly, the manufacturing method opens the doors to a new technology of rechargeable lithium batteries, which we can call self-supported (supported anode or cathode supported) depending on who is the element (anode or cathode) that structurally supports the components of the electrochemical cell
     35
    It also opens the doors to develop technologies called “All solid state batteries” or batteries where electrolytes are not used, which contain liquid solvents and therefore capable of working at temperatures above 200ºC. DESCRIPTION OF THE INVENTION 5

    The invention relates to an electrode with high thicknesses, of lithium ceramic material, absent from polymeric binders (additives) and their use in rechargeable batteries. Also, the invention relates to the manufacturing process thereof by means of powder extrusion molding technology. 10

    This procedure allows to manufacture electrodes (anodes or cathodes) with thicknesses of active material between 150 and 2000 microns, and therefore with high load that allows to increase the energy stored in the batteries. In particular, the high capacity value per unit area supplied by some of the assembled cells 15 (up to 12.7 mAh / cm2) is highlighted. This value has been achieved thanks to the high thickness of the ceramic sheets and therefore the high load of active material (~ 115 mg / cm2) that is achieved using the extrusion method presented.

    Another important technological advantage of the ceramic electrodes of this patent is that by eliminating the polymers used as binders in commercial batteries, it is possible to manufacture batteries capable of working at temperatures significantly higher than the current ones, not limiting the operating temperature to the degradation temperature. of these binders, without loss of performance, which translates into greater thermal stability, greater mechanical stability and an improvement in battery safety. In addition, they can be used with inorganic, polymeric solid electrolytes and also with high temperature boiling liquid electrolytes or with ionic liquids.

    Therefore, a first aspect of the invention relates to an electrode where the active electrode material is selected from a mixed lithium oxide and a lithium phosphate, characterized by having a thickness in a range of between 50 µm and 2000 µm, and a density in a range between 2.2 and 4.0 g / cm3.

     35

    In a preferred embodiment, the mixed oxide with lithium is selected from:
    a) mixed lithium and titanium oxides of general formula LixTiyOz, where x, y, z are in a range of between 0.01 and 1;
    b) mixed oxides of lithium, manganese and metallic elements with spinel structure of general formula LixMn2-yMyO4-z, 5
    where x is in a range between 0.9 and 1.15;
    and is in a range between 0.01 and 1;
    z is in a range between 0.0 and 1; Y
    M comprises one or more elements selected from the group consisting of nickel (Ni), chromium (Cr), cobalt (Co), titanium (Ti), iron (Fe), copper (Cu), zinc 10 (Zn), aluminum ( Al), tin (Sn), and vanadium (V);
    c) mixed oxides of lithium, cobalt and metallic elements with a laminar structure of general formula LixCo1 – yMyO2,
    where x is in a range between 0.9 and 1.15;
    and is in a range between 0 and 1; and 15
    M comprises one element or more elements selected from the group consisting of nickel (Ni), chromium (Cr), manganese (Mn), aluminum (Al), titanium (Ti), iron (Fe), copper (Cu), zinc ( Zn), tin (Sn), and vanadium (V).

    In a more preferred embodiment, the mixed oxide with lithium is a mixed oxide of lithium and titanium of general formula LixTiyOz, where x, y, z are in a range of between 0.01 and 1; more preferably, where X and Y are in a range between 0.1 and 0.8; even more preferably, the mixed lithium titanium oxide is Li4Ti5O12.

    In another embodiment, the lithium phosphate is a lithium, iron and metal elements phosphate with olivine structure of general formula LiFe1-yMy (PO4), where and is in a range between 0 and 1; and M comprises one element or more elements selected from the group consisting of nickel (Ni), chromium (Cr), manganese (Mn), cobalt (Co), aluminum (Al), titanium (Ti), iron (Fe), copper (Cu), zinc (Zn), and tin (Sn).
     30
    In another preferred embodiment, the electrode of the invention has a thickness in a range of between 450 and 1000 µm.

    In another preferred embodiment, the electrode of the invention has a density in the range of 2.5 to 4.0 g / cm 3. 35

    In another preferred embodiment, the electrode of the invention consists of a ceramic sheet characterized in that there is no binder present, it has a thickness in a range between 50 µm and 2000 µm, and a density in a range between 2.2 and 4.0 g / cm3. More preferably, the ceramic sheet has a thickness in a range of between 450 and 1000 µm and a density in a range of between 2.5 and 4.0 g / cm3.

    In a second aspect, the invention relates to the use of the electrode of the invention for the manufacture of a primary or secondary electrochemical cell, and more preferably a rechargeable lithium battery or a rechargeable lithium battery system 10 comprising at least one electrode as described above, an electrolyte compatible therewith, a separator located between the anode and the cathode, and two current collectors on which the electrodes are arranged.

    By "compatible electrolyte" is meant with the ceramic electrodes of the invention, an electrolyte that has a high conductivity of Li + ions, which is an electronic insulator and has high electrochemical stability. In a preferred embodiment, this electrolyte comprises a lithium salt dissolved in an organic solvent or in an ionic liquid.
     twenty
    In a more preferred embodiment said organic solvent may be selected from the group comprising: propylene carbonate, ethylene carbonate, fluoroethylene carbonate, butylene carbonate, dimethyl carbonate, diethyl carbonate, ethyl methyl carbonate, methyl propyl carbonate, ethylpropyl carbonate, methyl isopropyl carbonate, dipropyl carbonate, dibutyl carbonate, benzonitrile, acetonitrile, tetrahydrofuran, 2-methyltetrahydrofuran, γ-butyrolactone, 1,3-dioxolane, 4-methyl-1,3-dioxolane, N, N-dimethyl Formamide, dimethylacetamide, N-methylformamide, methylacetamide, N, N, N ', N'-tetraethylsulfonamide, dimethyl sulfoxide, dioxane, 1,2-dimethoxyethane, sulfolane, fluorocarbamate, nitrobenzene, diethylene glycol dimethyl ether, and mixtures thereof. More preferably, the organic solvent is a mixture of ethylene carbonate and dimethyl carbonate.

    In another preferred embodiment the ionic liquid may be selected from PYR1A (N-alkyl-N-methylpyrrolidinium) -TFSI (bis (trifluoromethanesulfonyl) imide), PYR1A-FSI (bis (fluorosulfonyl) imide), and the mixture of both. 35

    In another preferred embodiment, the lithium salt is selected from LiPF6, LiBF4, LiSbF6, LiAsF6, LiClO4, LiCF3SO3, Li (CF3SO2) 2N, LiC4F9SO3, LiAlO2, LiAICl4, LiN (CxF2x + 1SO2) (CyF2y + 1SO2 (CyF2y + 1SO2) x and y are natural numbers), Li (CF3SO2) 3C, Li (CN) 3C, LiCl, Lil, and mixtures thereof. More preferably, the lithium salt is selected from LiPF6 and Li (CF3SO2) 2N. 5

    By "separator" is meant an electronic insulating material, with high mechanical resistance, high chemical resistance and high wettability by liquid electrolyte. In a preferred embodiment, the separator is a fiberglass membrane or a macro or microporous polymer, generally in the form of a sheet, film or the like made from polymers such as polypropylene, polyethylene, fiberglass, polyester, polytetrafluoroethylene (PTFE), polyimide, polyethersulfone, or combinations thereof. The pores of these separators are filled with liquid electrolyte. The separator can also be non-porous. In this case, the separator swells in contact with the liquid electrolyte, and the polymer is selected from homopolymer or copolymers of ethylene oxide (POE), PVdF-HFP copolymers, polyacrylonitrile or polymethacrylonitrile, and combinations thereof.

    "Current collector" means a material with high electronic conductivity, high mechanical resistance and high chemical resistance. In a preferred embodiment, the current collectors are one or more metal elements such as copper, aluminum, nickel in the form of sheets, meshes or foams or carbonaceous materials with high electronic conductivity.

    By "a system of rechargeable lithium batteries" or "stackable batteries" is meant a set of batteries that results from electrically connecting in series and / or parallel the batteries of the invention. Said system, usually known as a battery stack, must have adequate voltage, intensity, energy density and / or power values for the application in which it is used. These lithium rechargeable battery systems are especially interesting since, for example, they are the ones needed for electric vehicles.

    A third aspect of the invention relates to the electrode manufacturing process as described above, which comprises the following steps:
    (i) mixing the active electrode material selected from a mixed lithium oxide or a lithium phosphate, in powder form, with a polymeric binder;
    (ii) granulating the extrudable mixture obtained in step i) to obtain the pellet that feeds the extruder;
    (iii) extrusion of the granulate from step ii) to obtain an electrode of desired thickness and dimensions;
    (iv) removal of the binder; and 5
    (v) sintering at a temperature between 750 and 1250 ° C, in an atmosphere selected from an oxidizing atmosphere (air, oxygen), inert (Argon, nitrogen), and reducing (nitrogen, argon or N2 / Ar / H2 mixtures in varying amounts).
     10
    In a preferred embodiment, the removal of the binder takes place by means of a combined cycle comprising a first solvent removal stage, such as n-heptane, at 50 ° C for 3 h, followed by another thermal removal stage, in which The product obtained in the previous stage is subjected to 200 ° C and subsequently to 450 ° C. In the solvent removal stage the extraction of the wax and stearic acid occurs, and in the second stage the degradation of the polypropylene essentially takes place.

    In the present invention, "polymeric binder" or binder systems is understood as any of the polymers usually used for thermoplastic extrusion molding mixed with waxes, such as paraffin, and other additives, such as stearic acid. These polymers can be selected from the group consisting of polypropylene homopolymers and copolymers, high and low density polyethylene homopolymers and copolymers, homopolymers and copolymers of polyethylene vinyl acetate, polystyrene, polyvinylchloride, ethylene polyterephthalate, polyamides, 25 polymethacrylate of methyl, polycarbonate, polymethacrylonitrile, polyacrylonitrile, polyaniline, or mixtures thereof.

    In a preferred embodiment, the "polymeric binder" is a mixture of polypropylene, paraffin wax and stearic acid. 30

    In another embodiment of the invention, one or more carbonaceous materials in powder form, such as carbon black, or in the form of fibers, such as carbon nanotubes, or in the form of sheets can be added to the polymeric binder , such as graphene materials, in an amount sufficient to reach the percolation of carbonaceous materials, and as a consequence
    ensure adequate electronic conductivity in the ceramic sheet. In another preferred embodiment, metal powders, such as silver or copper, could be added instead of the carbonaceous material or in addition thereto.

    Throughout the description and the claims the word "comprises" and its 5 variants are not intended to exclude other technical characteristics, additives, components or steps. For those skilled in the art, other objects, advantages and features of the invention will be derived partly from the description and partly from the practice of the invention. The following examples and figures are provided by way of illustration, and are not intended to be limiting of the present invention. 10
    BRIEF DESCRIPTION OF THE FIGURES

    FIG. 1.- Scheme of the powder extrusion molding process. Initially the active material is mixed in powder form with a polymeric binder. This mixture, called "feedstock", is subjected to a pelletizing process to favor its incorporation into the extruder. The extrusion is carried out in a conventional plastic extruder obtaining the desired shape. Subsequently, the polymeric binder is removed and finally the ceramic electrode is sintered in a controlled atmosphere. twenty

    FIG. 2.- Comparison of the discharge curves of a ceramic electrode of Li4Ti5O12 (without polymer binders) manufactured by the extrusion method of this patent at 1000ºC (475 µm, 141 mg / cm2) and a control electrode (with polymeric binders and carbon black) with high thickness (122 µm, 16 mg / cm2) processed by the conventional "tape casting" method on a copper current collector. The experiment was carried out at a constant current intensity of 7.3 mA / g (C / 24) and 30 ° C.

    FIG. 3.- (a) Selection of discharge curves recorded during the cycling of the 30 Li4Ti5O12 ceramic electrode manufactured by extrusion and subsequently sintered at 1000 ° C using a constant current intensity of 7.3 mA / g in charge and discharge. (b) Comparison of the variation of the volumetric capacity of the ceramic electrode of Li4Ti5O12 manufactured by extrusion and the control electrode during the 30 ° C cycling study between 2.7 and 1V. 35
    EXAMPLES

    The invention will now be illustrated by tests carried out by the inventors, which demonstrates the effectiveness of the product of the invention.
     5
    Example 1. Electrode manufacturing

    In the powder extrusion molding process that has been developed (process steps in Figure 1), 95 g of Li4Ti5O12 powder is initially mixed with a polymeric binder (10 g of polypropylene, 9 g of paraffin wax and 1 g stearic acid) 10 to 170 ºC and 40 rpm This mixture, called "feedstock", is subjected to a pelletizing process to favor its incorporation into the extruder. The extrusion is carried out in a conventional plastic extruder obtaining the desired sheet shape with a thickness close to 1 mm. Subsequently, the polymeric binder is removed in two stages. Initially, the sheets are immersed in n-heptane 15 at 50 ° C for 3 h, and then subjected to a thermal cycle up to 450 ° C to completely remove the binder. Finally, the ceramic electrode is sintered in an atmosphere of Ar-5% H2 at 1000 ºC for 1h.

    Example 2. Electrochemical studies of electrodes 20

    The ceramic electrodes that have been manufactured in Example 1 have been tested in airtight cells with a button cell type format. These cells are formed by: 1) a copper current collector in direct contact with the self-supporting ceramic electrode of Li4Ti5O12, 2) a 1M solution of the lithium salt LiPF6 dissolved in a 1: 1 mixture by weight of ethylene carbonate and dimethyl carbonate, which is embedded in a fiberglass separator, and 3) a metallic lithium sheet as a negative electrode.

    In order to demonstrate the technological advantages of the spinel ceramic electrodes 30 Li4Ti5O12 object of the present patent, control electrodes have been manufactured using powder of the same commercial sample of Li4Ti5O12 as active electrode material. These electrodes have been prepared in the same way that rechargeable Li-ion battery electrodes are commercially prepared.
     35
    The formulation of the manufactured control electrodes has been 80% by weight of Li4Ti5O12, 10% carbon black and 10% polyvinylidene fluoride polymer (PVDF). All these components of the composite electrode have been deposited on copper or aluminum sheets. It has been used as a control electrode that with the greatest thickness (122 µm) manufactured and that has not presented any fracture in its entire surface.

    Figure 2 shows the discharge curves of a ceramic anode of Li4Ti5O12 of 470 µm thick and 141 mg / cm2 in weight and the control electrode (122 µm thick and 16 mg / cm2 of Li4Ti5O12) recorded for a current 10 7.3 mA / g constant (C / 24). The comparative study of the curves obtained demonstrates that the electrode manufactured in this patent is capable of storing almost three times the electricity per unit volume (326 mAh / cm3) than the control electrode (116 mAh / cm3). The improvement is even greater when comparing capacity per unit area. Thus, the electrode manufactured using the extrusion method that we have developed for this patent has a capacity of 12.7 mAh / cm2 being for the control electrode of 1.4 mAh / cm2. Therefore, for this electrochemical parameter the increase is by a factor of 10 times. The working voltage of the ceramic electrode object of this patent and that of the control electrode are close to each other, its value being 1.5V. In both cases the voltage remains virtually unchanged 20 during electrode operation (Figure 2). An important technological aspect is that these voltage values prevent the formation of the dangerous lithium dendrites that occurs in commercial batteries with graphite anodes, greatly increasing the safety of the battery.
     25
    The electrochemical behavior of the ceramic electrodes of Li4Ti5O12 during successive charge / discharge cycles has also been studied. A selection of discharge curves recorded during the cycling of a ceramic electrode manufactured according to Example 1 and with a spinel charge of 141 mg / cm2 is shown in Figure 3.a. The successive charge / discharge cycles were carried out at a constant current intensity of 7.3 mA / g (C / 24), 30 ° C and in the voltage range from 2.7 V to 1 V.

    As can be seen in Figure 3.a, the curves for the different cycles are analogous, with only a small decrease in the specific capacity being observed as the number of completed cycles increases. This result shows that
    Ceramic electrodes of Li4Ti5O12 object of the present patent cycle effectively. Figure 3.b compares the cycling behavior of the ceramic electrode with the control composite electrode. After 25 discharge / charge cycles, the ceramic electrode is capable of supplying 312 mAh / cm3; that is, the electrode has retained 95.7% of its nominal capacity (326 mAh / cm3) after the cycling study. 5 This result is very important as it demonstrates that the ceramic electrode of Li4Ti5O12 maintains its electrochemical activity in cycling.

    When compared to the control electrode, it is clearly seen how the reversible capacity of the ceramic electrode (320 mAh / cm3) is much higher than the control electrode (115 mAh / cm3). In conclusion, the electrochemical studies carried out allow to demonstrate that the Li4Ti5O12 spinel ceramic electrode manufactured by the extrusion method can be used as an anode in rechargeable high-energy lithium batteries and with improved safety. The specific electrochemical performance of this electrode is clearly superior to the control electrode 15 manufactured by the conventional method and using the same commercial sample of Li4Ti5O12 as active material.
    权利要求:
    Claims (26)
    [1]

    1. Electrode for batteries where the active electrode material is selected from a mixed lithium oxide or a lithium phosphate, characterized in that it has a thickness in a range between 50 µm and 2000 µm, and a density 5 in a range between 2.2 and 3.6 g / cm3.

    [2]
    2. Electrode according to claim 1 wherein the mixed lithium oxide is selected from:
    a) mixed lithium and titanium oxides of the general formula LixTiyOz, where x, y, z are in a range of between 0.01 and 1;
    b) mixed oxides of lithium, manganese and metallic elements with spinel structure of general formula LixMn2-yMyO4-z,
    where x is in a range between 0.9 and 1.15;
    and is in a range between 0 and 1; fifteen
    z is in a range between 0 and 1; Y
    M comprises one or more elements selected from the group consisting of nickel (Ni), chromium (Cr), cobalt (Co), titanium (Ti), iron (Fe), copper (Cu), zinc (Zn), aluminum (Al ), tin (Sn), and vanadium (V);
    c) mixed oxides of lithium, cobalt and metallic elements with a laminar structure of 20 general formula LixCo1 – yMyO2,
    where x is in a range between 0.9 and 1.15;
    and is in a range between 0 and 1; Y
    M comprises one element or more elements selected from the group consisting of nickel (Ni), chromium (Cr), manganese (Mn), aluminum (Al), titanium (Ti), iron (Fe), copper (Cu), zinc (Zn), tin (Sn), and vanadium (V).
    d) lithium phosphate, iron and metal elements with olivine structure of general formula LiFe1-yMy (PO4),
    where and is in a range between 0 and 1; Y
    M comprises one element or more elements selected from the group consisting of nickel (Ni), chromium (Cr), manganese (Mn), cobalt (Co), aluminum (Al), titanium (Ti), iron (Fe), copper (Cu), zinc (Zn), and tin (Sn).

    [3]
    3. Electrode according to any of the preceding claims wherein the mixed lithium oxide is a mixed lithium and titanium oxide of the general formula LixTiyOz, wherein X, Y, Z are in a range between 0.1 and 0.8 .

    [4]
    4. Electrode according to any of the preceding claims wherein the mixed lithium oxide 5 is Li4Ti5O12.

    [5]
    5. Electrode according to any of the preceding claims characterized in that its thickness is in a range between 450 and 1000 µm.
     10
    [6]
    6. Electrode according to any of the preceding claims consisting of a ceramic sheet free of organic components.

    [7]
    7. Electrode according to any of the preceding claims wherein the mixed lithium oxide is Li4Ti5O12 and acts as an anode. fifteen

    [8]
    8. Method of manufacturing the electrode according to any of the preceding claims, comprising the following steps:
    (i) mixing the active electrode material that is selected from a mixed lithium oxide or a lithium phosphate, in powder form, with a polymeric binder;
    (ii) granulating the extrudable mixture obtained in step i) to obtain the pellet that feeds the extruder;
    (iii) extrusion of the granulate from step ii) to obtain an electrode of desired thickness and dimensions; 25
    (iv) removal of the binder; Y
    (v) sintering at a temperature between 750 and 1250 ° C in an atmosphere selected from oxygen, air, argon, nitrogen, argon-nitrogen mixtures, and nitrogen-hydrogen mixtures.
     30
    [9]
    9. Process according to claim 8, wherein the active powder of step i) is a mixed lithium titanium oxide.

    [10]
    10. The method according to claim 9, wherein the active powder of step i) is Li4Ti5O12. 35

    [11]
    Method according to any one of claims 8 to 10, wherein the polymeric binder of step i) is a thermoplastic material selected from polypropylene homopolymers and copolymers, high and low density polyethylene homopolymers and copolymers, polyethylene homopolymers and copolymers. -vinyl acetate, polystyrene, polyvinylchloride, ethylene polyterephthalate, 5 polyamides, methyl polymethacrylate, polycarbonate, polyacrylonitrile, polyaniline, or mixtures thereof, optionally mixed with waxes and other additives.

    [12]
    12. Method according to claim 11 wherein the polymeric binder is a mixture of polypropylene, paraffin wax and stearic acid. 10

    [13]
    13. Method according to any of claims 11 or 12, wherein one or more carbonaceous materials in the form of powder, fibers or sheets are added to the polymeric binder.
     fifteen
    [14]
    14. Method according to claim 11, wherein the carbonaceous material is carbon black.

    [15]
    15. A method according to any of claims 8 to 14 wherein the removal of the binder from step (iv) takes place by means of a combined cycle comprising a first stage of solvent removal at 50 ° C for 3 h, followed by a phase of elimination thermal, in which the product obtained from the previous stage is subjected to 200 ° C and subsequently to 450 ° C.

    [16]
    16. Use of the electrode according to any one of claims 1 to 7 as part of a primary or secondary electrochemical cell.

    [17]
    17. Use of the electrode according to claim 16 wherein the electrochemical cell is a rechargeable lithium battery or a rechargeable lithium battery system.
     30
    [18]
    18. Rechargeable lithium battery comprising at least one electrode according to any one of claims 1 to 7 supported on a current collector with high electronic conductivity, an electrolyte, and a separator located between the anode and the cathode, and where the anode is the electrode according to any one of claims 1 to 7. 35

    [19]
    19. Rechargeable lithium battery according to claim 18 wherein the electrolyte comprises a lithium salt dissolved in an organic solvent or in an ionic liquid.

    [20]
    20. Rechargeable lithium battery according to claim 19 wherein the organic solvent comprises a mixture of ethylene carbonate and dimethyl carbonate.

    [21]
    21. Rechargeable lithium battery according to claim 19 wherein the ionic liquid is selected from the group comprising N-alkyl-N-methylpyrrolidinium-bis (trifluoromethanesulfonyl) imide, bis (fluorosulfonyl) imide, and the mixture of both. 10

    [22]
    22. Rechargeable lithium battery according to any of claims 18 to 21 wherein the lithium salt is selected from LiPF6, LiBF4, LiSbF6, LiAsF6, LiClO4, LiCF3SO3, Li (CF3SO2) 2N, LiC4F9SO3, LiAlO2, LiAICl4, LiN (CxF2x + 1SO2) (CyF2y + 1SO2) where x and y are natural numbers, Li (CF3SO2) 3C, Li (CN) 3C, LiCl, Lil, and the mixtures thereof.

    [23]
    23. Rechargeable lithium battery according to claim 22 wherein the lithium salt is selected from LiPF6 and Li (CF3SO2) 2N.
     twenty
    [24]
    24. Rechargeable lithium battery according to any of claims 18 to 23 wherein the separator is a porous polymer, which is selected from polypropylene, polyethylene, fiberglass, polyester, polytetrafluoroethylene (PTFE), polyimide, polyethersulfone, and combinations thereof. same.
     25
    [25]
    25. Rechargeable lithium battery according to any of claims 18 to 23 wherein the separator is a non-porous polymer, which is selected from homopolymer or copolymers of ethylene oxide (POE), PVdF-HFP copolymers, polyacrylonitrile or polymethacrylonitrile, and combinations thereof.
     30
    [26]
    26. Rechargeable lithium battery system comprising at least one battery according to any of claims 18 to 25.
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    公开号 | 公开日
    EP3432390A1|2019-01-23|
    ES2633149B2|2018-06-06|
    WO2017158223A1|2017-09-21|
    US20190173083A1|2019-06-06|
    EP3432390A4|2019-12-11|
    US11121366B2|2021-09-14|
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    JP6040489B2|2011-10-29|2016-12-07|日本ケミコン株式会社|Sheet composite, production method thereof, electrode and electrochemical element using the sheet composite|
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    FR2989378B1|2012-04-16|2015-10-02|Commissariat Energie Atomique|POLYMER AS ELECTRODE MATERIAL FOR LITHIUM SECONDARY BATTERIES.|CN107706410B|2017-11-23|2020-06-09|宁夏汉尧石墨烯储能材料科技有限公司|Preparation method of double-atmosphere roasting dynamic coating lithium-rich ternary lithium ion battery positive electrode material|
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    EP17765906.7A| EP3432390A4|2016-03-16|2017-03-16|Electrodes for rechargeable lithium batteries|
    US16/085,371| US11121366B2|2016-03-16|2017-03-16|Electrodes for rechargeable lithium batteries|
    PCT/ES2017/070149| WO2017158223A1|2016-03-16|2017-03-16|Electrodes for rechargeable lithium batteries|
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