Patent Application
20130084492
1. Field of the Invention
The present invention relates to a non-aqueous electrolyte secondary battery. The present invention relates to a non-aqueous electrolyte secondary battery including a polyanionic positive electrode material and lithium nickel composite oxide as positive electrode active materials.
2. Related Art
Non-aqueous electrolyte secondary batteries such as lithium ion secondary batteries are currently used as power sources of electric appliance and the like, and furthermore, as power sources of electronic automobiles (such as EVs (electric vehicles), HEVs (hybrid electric vehicles) and the like). In addition, non-aqueous electrolyte secondary batteries such as lithium ion secondary batteries require further improvement in characteristics, such as improvement in energy density (realization of high capacity), improvement in power density (realization of high power) and improvement in cycle characteristics (improvement in cycle lifespan), high safety and the like.
Recently, most of lithium ion secondary batteries used for small-sized electric appliances and the like use lithium composite oxide such as LiCoO2 as a positive electrode active material and realize electric storage devices with high capacity and long lifespan. However, these positive electrode active materials aggressively react with electrolytic solutions, generate heat while producing oxygen, and in the most serious cases, disadvantageously may cause combustion, in high temperature and high electric potential states when abnormal phenomena occur.
Recently, polyanionic positive electrode materials are researched as positive electrode active materials that exhibit superior thermal stability even in high temperature and high electric potential states. Among these positive electrode active materials, olivine-type Fe (LiMnPO4), olivine-type Mn(LiMnPO4) having similar crystalline structures and the like are researched and are partially practically applicable as electrically-driven tools. In addition, NASICON-type vanadium lithium phosphate such as Li3V2(PO4)3 attracts great attention as a similar positive electrode active material with superior thermal stability (for example, Patent Document 1: JPA-2001-500665).
However, polyanionic positive electrode materials should be surface-coated with conductive carbon due to low electrical conductivity. In this regard, coating conductive carbon on the surface of the active material causes problems such as increase in specific surface area and deterioration in cell characteristics due to moisture adsorption in the manufacturing environment.
In an attempt to solve these problems, Patent Document 2 (JP-A-2009-048981) discloses a non-aqueous electrolyte secondary battery comprising a positive electrode using a compound represented by formula of LixFe1-yMyPO4 (in which M is at least one selected from the group consisting of Co, Ni, Cu, Zn, Al, Sn, B, Ga, Cr, V, Ti, Mg, Ca and Sr; and 0.9<x<1.2, 2.0≦y<0.3) as a positive electrode active material, a negative electrode containing a lithium metal, a lithium alloy or a material capable of doping and dedoping lithium, and a non-aqueous electrolytic solution containing fluorinated ethylene carbonate. That is, Patent Document 2 also discloses a method for reducing deterioration in cells caused by moisture, when a polyanionic active material coated with conductive carbon is used for a positive electrode.
As described above, when a polyanionic active material coated with conductive carbon is used for a positive electrode, a specific surface area increases and cell characteristics are deteriorated due to moisture adsorption in the manufacturing environment. Patent Document 2 discloses adsorption of moisture in a cell, inhibition of generation of hydrogen fluoride during reaction with LiPF6 or the like in an electrolytic solution and inhibition of cell deterioration through incorporation of fluorinated ethylene carbonate (FEC) into a non-aqueous electrolytic solution. However, Patent Document 2 does not suggest a solution of hydrogen fluoride generated by reaction of fluorinated ethylene carbonate with moisture, thus disadvantageously causing a deterioration of cell characteristics due to the small amount of hydrogen fluoride.
One or more embodiments of the invention provide a non-aqueous electrolyte secondary battery including a positive electrode containing a polyanionic active material coated with conductive carbon and an electrolytic solution containing fluorinated ethylene carbonate, in which deterioration in properties caused by hydrogen fluoride generated by reaction of fluorinated ethylene carbonate with moisture is inhibited.
Hereinafter, embodiments of the present invention will be described in detail. The embodiments relate to a non-aqueous electrolyte secondary battery. Examples of the non-aqueous electrolyte secondary battery include lithium ion secondary batteries. As described below, the present invention is particularly not limited to other components except for the positive electrode in the non-aqueous electrolyte secondary battery and may be performed by suitably combining conventional techniques known in the art so long as the effects of the present invention are not impaired.
The non-aqueous electrolyte secondary battery according to one embodiment includes a positive electrode including a positive electrode mixture layer containing a positive electrode active material. The positive electrode active material includes a first active material in which LiFePO4, LiMnPO4 or Li3V2(PO4)3 is coated with a carbon as polyanionic positive electrode material and a second active material of lithium nickel composite oxide.
In the embodiments, LiFePO4, LiMnPO4 or Li3V2(PO4)3 may be prepared by any method without particular limitation. For example, Li3V2(PO4)3 may be prepared by a method including mixing a lithium source such as LiOH, or LiOH.H2O, a vanadium source such as V2O5 or V2O3 and a phosphate source such as NH4H2PO4 or (NH4)2HPO4, followed by reacting and baking and the like. Li3V2(PO4)3 may be in the form of a particle conventionally obtained by grinding the baked substance or the like.
In addition, LiFePO4 and LiMnPO4 may be for example prepared by mixing a lithium source such as lithium oxide, lithium carbonate or lithium hydroxide, a phosphorous source such as ammonium phosphate, ammonium hydrogen phosphate, or ammonium dihydrogen phosphate, a Fe source or a Mn source containing a Fe element or a Mn element such as oxalate, acetate, oxide, hydroxide, carbonate, sulfate or nitrate, followed by reacting, and baking and the like. Furthermore, phosphate lithium which is a compound serving as both a lithium source and a phosphorous source, or phosphate which is a compound serving as both a phosphorous source and a Fe source, or serving as both a phosphorous source and a Mn source may be used as a raw material. LiFePO4, LiMnPO4 or Li3V2(PO4)3 may be in the form of a particle obtained by grinding the baked substance or the like.
LiFePO4, LiMnPO4 or Li3V2(PO4)3 should be surface-coated with conductive carbon due to original low electrical conductivity. Accordingly, electrical conductivity of LiFePO4, LiMnPO4 or Li3V2(PO4)3 can be improved. The coating amount of conductive carbon is preferably 0.1 to 20% by mass in terms of C atom.
The conductive carbon coating may be performed by a well-known method. For example, the conductive carbon coating can be formed on the surface of LiFePO4, LiMnPO4 or Li3V2(PO4)3 by mixing conductive carbon with citric acid, ascorbic acid, polyethylene glycol, sucrose, methanol, propene, carbon black, Ketjen black or the like as a carbon coating material during reaction or baking in the production of LiFePO4, LiMnPO4 or Li3V2(PO4)3.
The particle sizes of LiFePO4, LiMnPO4 or Li3V2(PO4)3 particles are not particularly limited and those having the desired particle size may be used. Since the particle size affects stability or density of LiFePO4, LiMnPO4 or Li3V2(PO4)3, D50 in the particle size distribution of secondary particles of LiFePO4, LiMnPO4 or Li3V2(PO4)3 is preferably 0.5 to 25 μm. When D50 is lower than 0.5 μm, contact area with the electrolytic solution increases and stability of LiFePO4, LiMnPO4 or Li3V2(PO4)3 may be deteriorated, and when the D50 exceeds 25 μm, power may be deteriorated due to deterioration in density. When D50 falls within the range, electric storage devices with superior stability and higher power can be obtained. In the particle size distribution of secondary particles of LiFePO4, LiMnPO4 or Li3V2(PO4)3, D50 is more preferably 1 to 10 μm, particularly preferably 3 to 5 μm. Furthermore, in the particle size distribution of secondary particles, D50 is a value measured using a particle size distribution meter based on a laser diffraction (light scattering) manner.
Various lithium nickel composite oxides may be used in the embodiments. In one embodiment, as lithium nickel composite oxide of the second active material, for example, LiNi0.8Co0.2O2, LiNi0.8Co0.1Mn0.1O2, LiNi0.6Co0.2Mn0.2O2, and LiNi0.3Co0.3Mn0.4O2 which are lithium nickel cobalt composite oxides, are used. Here, the content of Ni element in the lithium nickel composite oxide affects proton absorption force of lithium nickel composite oxide. In the embodiments, the Ni element inhibits elution of iron, manganese or vanadium from LiFePO4, LiMnPO4 or Li3V2(PO4)3 and is generally used to inhibit generation of hydrogen fluoride by fluorinated ethylene carbonate and moisture. The amount of nickel contained in the second active material is preferably a value that satisfies the case in which x is 0.3 to 0.8 when the second active material is represented by LiNixCoyMzO2 (in which x+y+z=1, x>0). When LiNi0.8Co0.2O2 or LiNi0.8Co0.1Mn0.1O2 is used as the second active material, the content thereof in the positive electrode is adjusted to 10 to 80 parts by mass, thereby satisfying the limited amount of nickel. When LiNi0.6Co0.2Mn0.2O2 is used as the second active material, the content thereof in the positive electrode is adjusted to 15 to 85 parts by mass, thereby satisfying the limited amount of nickel. When LiNi0.3Co0.3Mn0.4O2 is used as the second active material, the content thereof in the positive electrode is adjusted to 50 to 85 parts by mass, thereby satisfying the limited amount of nickel.
In addition, in the lithium nickel composite oxide of the embodiments, a metal element different from Ni, having an atomic number of 11 or higher may be substituted into the Ni site. The metal element different from Ni, having an atomic number of 11 or higher, is preferably selected from transition metal elements. The transition elements may have a plurality of oxidation numbers like Ni, thus using the oxidation and reduction range in the lithium nickel composite oxide and maintaining high capacity properties. The metal element different from Ni, having an atomic number of 11 or higher, is for example Co, Mn, Al or Mg, preferably Co or Mn.
The lithium nickel composite oxide may be prepared by any method without particular limitation. For example, the lithium nickel composite oxide may be prepared by mixing a synthesized Ni-containing precursor and a lithium compound at a desired stoichiometric ratio by a solid phase reaction method, a co-precipitation method, a sol gel method or the like, followed by baking under an air atmosphere or the like.
The lithium nickel composite oxide may be commonly in the form of a particle obtained by grinding the baked substance. The particle size thereof is not particularly limited and those having the desired particle size may be used. Since the particle size affects stability or density of lithium nickel composite oxide, the mean particle size of particles is preferably 0.5 to 25 μm. When the mean particle size is lower than 0.5 μm, a contact area with the electrolytic solution increases and stability of lithium nickel composite oxide may be deteriorated. When the mean particle size exceeds 25 μm, power may be deteriorated due to deterioration in density. When the mean particle size falls within the range, electric storage devices with superior stability and higher power can be obtained. The mean particle size of particles of lithium nickel composite oxide is more preferably 1 to 25 μm, particularly preferably 5 to 20 μm. Furthermore, the mean particle size of these particles is a value measured using a particle size distribution meter based on a laser diffraction (light scattering) manner.
The positive electrode of the embodiments may be produced using well-known materials as far as the positive electrode active materials include at least one of LiFePO4, LiMnPO4 and Li3V2(PO4)3 which are coated with carbon as described in the above and lithium nickel composite oxide. Specifically, production of the positive electrode will be described in detail below.
A positive electrode mixture layer is formed by a process including applying a positive electrode slurry obtained by dispersing a mixture containing the positive electrode active material, a binder, a conductive agent in a solvent to a positive electrode collector and drying the applied substance. After drying, pressing may be performed. As a result, the positive electrode mixture layer is uniformly and firmly pressed on the collector. The positive electrode mixture layer preferably has a thickness of 10 to 200 μm, preferably 20 to 100 μm.
The binder used for formation of the positive electrode mixture layer is for example a fluorine-containing resin such as polyvinylidene fluoride, an acrylic binder, a rubber-based binder such as SBR, a thermoplastic resin such as polypropylene and polyethylene, carboxymethylcellulose or the like. The binder is preferably a fluorine-containing resin or a thermoplastic resin that is chemically and electrochemically stable to non-aqueous electrolytic solution used for electric storage devices of the embodiments, particularly preferably a fluorine-containing resin. Examples of the fluorine-containing resin include polyvinylidene fluoride as well as polytetrafluoroethylene, vinylidene fluoride-trifluoroethylene copolymers, ethylene-tetrafluoroethylene copolymers and propylene-tetrafluoroethylene copolymers and the like. The content of the binder is preferably 0.5 to 20% by mass with respect to the positive electrode active material.
The conductive agent used for formation of the positive electrode mixture layer is for example conductive carbon such as carbon black (CB), a metal such as copper, iron, silver, nickel, palladium, gold, platinum, indium or tungsten, or conductive metal oxide such as indium oxide and tin oxide. The content of conductive material is preferably 1 to 30% by mass with respect to the positive electrode active material.
The solvent used for the formation of the positive electrode mixture layer may be water, isopropyl alcohol, N-methylpyrrolidone (NMP), dimethylformamide or the like.
The surface of the positive electrode collector that contacts the positive electrode mixture layer is a conductive base material having conductivity and the positive electrode collector is for example a conductive base material made of a conductive material such as metal, conductive metal oxide or conductive carbon, or a non-conductive base material coated with a conductive material. The conductive material is preferably copper, gold, aluminum or an alloy thereof or conductive carbon. The positive electrode collector may be an expended metal, a punched metal, a foil, a mesh, a foamed material or the like of the material. In cases of porous materials, the shape or number of through holes is not particularly limited and may be suitably determined so long as the movement of lithium ions is not inhibited.
The content of second active material, LiNi0.8Co0.1Mn0.1O2, is 10 to 80 parts by mass with respect to the active material of positive electrode according to one embodiment. In another embodiment, the content of the second active material, LiNi0.6Co0.2Mn0.2O2, is 15 to 80 parts by mass with respect to the positive electrode active material. In another embodiment, the content of the second active material, LiNi0.3Co0.3Mn0.4O2, is 50 to 85 parts by mass with respect to the positive electrode active material. As a result, the amount of nickel is defined. When the content of nickel is excessively low, inhibition effects of elution of vanadium from Li3V2(PO4)3 is not sufficiently exerted and superior cycle properties cannot be obtained. In addition, high capacity cannot be obtained. On the other hand, when the content of nickel is excessively high, elution of vanadium from Li3V2(PO4)3 can be inhibited, but charge and discharge cycle properties of electric storage devices may be not sufficiently improved. In the embodiments, the Ni element has an activity capable of inhibiting elution of vanadium from Li3V2(PO4)3 as described in the above, and at the same time, is used for inhibition of hydrogen fluoride by fluorinated ethylene carbonate and moisture.
The negative electrode of the embodiments is not particularly limited and may be prepared using a well-known material. For example, a negative electrode slurry obtained by dispersing a mixture containing a generally used negative electrode active material and a binder in a solvent is applied to a negative electrode collector, followed by drying to form a negative electrode mixture layer. Furthermore, the binder, the solvent and the collector may be the same as in the aforementioned positive electrode.
The negative electrode active material is for example a lithium-based metal material, a inter-metal compound material of a metal and a lithium metal, a lithium compound or lithium intercalation carbon material or the like.
Examples of lithium-based metal material include metal lithium and lithium alloys (for example, Li—Al alloys). The inter-metal material of the metal and the lithium metal is for example an inter-metal compound including tin, silicon or the like. The lithium compound is for example lithium nitride.
In addition, examples of the lithium intercalation carbon material include graphite, carbon-based materials such as hard carbon materials, polyacene materials and the like. The polyacene material is for example insoluble and unmeltable PAS having a polyacene skeleton. Furthermore, these lithium intercalation carbon materials are substances that are capable of reversibly doping lithium ions. The negative electrode mixture layer generally has a thickness of 10 to 200 μm, preferably 20 to 100 μm.
In addition, in the embodiments, a coating concentration of the negative electrode mixture layer is suitably designed based on a coating concentration of the positive electrode mixture layer. Commonly, the lithium ion secondary battery is designed such that capacities (mAh) of the positive electrode and the negative electrode are substantially equivalent in view of capacity balance of positive electrode and negative electrode, or energy density. Accordingly, the coating concentration of negative electrode mixture layer is determined depending on the type of negative electrode active material, capacity of positive electrode or the like.
The non-aqueous electrolytic solution of the embodiments may be used without particular limitation so long as it contains fluorinated ethylene carbonate and may be a well-known material. For example, an electrolytic solution obtained by dissolving a general lithium salt as an electrolyte in an organic solvent may be used in that it does not cause electrolysis even at a high voltage and lithium ions can be stably present.
Examples of fluorinated ethylene carbonate (FEC) include 4-fluoro-1,3-dioxolan-2-one, 4,4-difluoroethylene carbonate, 4,5-difluoroethylene carbonate, 4,4,5-trifluoroethylene carbonate, 4,4,5,5-tetrafluoroethylene carbonate and the like.
The content of the fluorinated ethylene carbonate in the non-aqueous electrolytic solution is preferably 0.2% by mass to 10% by mass. When the content is 0.2% by mass or higher, cycle properties can be improved. When the content is 10% by mass or higher, the fluorinated ethylene carbonate remains, thus causing deterioration due to environmental moisture and positively affecting cycle properties and the like.
Examples of the electrolyte include CF3SO3Li, C4F9SO8Li, (CF3SO2)2NLi, (CF3SO2)3CLi, LiBF4, LiPF6, LiClO4 and combinations thereof.
Examples of the organic solvent include propylene carbonate, ethylene carbonate, buthylene carbonate, dimethyl carbonate, diethyl carbonate, ethylmethyl carbonate, vinyl carbonate, trifluoromethyl propylene carbonate, 1,2-dimethoxyethane, 1,2-diethoxyethane, γ-butyrolactone, tetrahydrofuran, 1,3-dioxolane, 4-methyl-1,3-dioxolane, diethylether, sulfolan, methylsulfolan, acetonitrile, propionitrile and mixtures thereof.
The concentration of electrolyte in the non-aqueous electrolytic solution is preferably 0.1 to 5.0 mol/L, more preferably, 0.5 to 3.0 mol/L.
The non-aqueous electrolytic solution may be a liquid state, a solid electrolyte or a polymer gel electrolyte in which a plasticizer or polymer is incorporated.
The separator used in the embodiments is not particularly limited and may be a well-known separator. For example, a porous material that exhibits durability to an electrolytic solution, a positive electrode active material and a negative electrode active material, has communication holes and has no electrical conductivity is preferably used. Examples of this porous material include woven fabrics, non-woven fabrics, synthetic resin microporous membranes, glass fibers and the like. The synthetic resin microporous membrane is preferably used and a microporous membrane made of polyolefin such as polyethylene or polypropylene is particularly preferably used, in terms of thickness, membrane strength and membrane resistance.
Hereinafter, as an embodiment of non-aqueous electrolyte secondary battery, an example of lithium ion secondary battery will be described with reference to the drawings.
The positive electrode 21 includes a positive electrode mixture layer 21a containing a positive electrode active material of the embodiments and a positive electrode collector 21b. The positive electrode mixture layer 21a is disposed on the side surface of the separator 23 of the positive electrode collector 21b. The negative electrode 22 includes a negative electrode mixture layer 22a and a negative electrode collector 22b. The negative electrode mixture layer 22a is disposed on the side surface of the separator 23 of the negative electrode collector 22b. The positive electrode 21, the negative electrode 22, and the separator 23 are mounted in an exterior container (not shown) and the exterior container is filled with a non-aqueous electrolytic solution. Examples of the container include battery cans, laminate films and the like. The positive electrode collector 21b and the negative electrode collector 22b are optionally connected to leads for connections of exterior terminals (not shown).
Then,
Furthermore, the lithium ion secondary battery 30 may be provided with a lithium electrode to allow lithium ions to be freely doped into a positive electrode and/or a negative electrode. In this case, movement of lithium ions is facilitated, and the positive electrode collector 31b or the negative electrode collector 32b is provided with through holes that extend in the lamination direction of the electrode unit 34.
In addition, the lithium ion secondary battery 30 has a structure in which negative electrodes are arranged in the uppermost and the lowermost parts and is not limited to the structure. The lithium ion secondary battery 30 may have a structure in which positive electrodes are arranged in the uppermost and the lowermost parts.
Hereinafter, Examples will be described.
Examples 1 to 4 and Comparative Examples 1 to 3 are cases in which the second active material is LiNi0.8Co0.1Mn0.1O2.
The following substances for the positive electrode mixture layer were mixed to obtain a positive electrode slurry.
First active material (Li3V2(PO4)3); 80 parts by mass
Second active material (LiNi0.8Co0.1Mn0.1O2); 10 parts by mass
Binder (polyvinylidene fluoride (PVdF)); 5 parts by mass
Conductive agent (carbon black); 5 parts by mass
Solvent (N-methyl2-pyrrolidone (NMP)); 100 parts by mass
The positive electrode slurry was applied to a positive electrode collector of an aluminum foil (thickness 30 μm), followed by drying to form a positive electrode mixture layer on the positive electrode collector. After formation of the positive electrode mixture layer, a coated region (region where the positive electrode mixture layer is formed) except an uncoated region with a size of 10×10 mm as a tab for lead connection was cut to a size of 50×50 mm. Li3V2(PO4)3 for the first active material used herein was coated with 1.4% by mass of carbon in terms of C atom.
The following substances for the negative electrode mixture layer were mixed to obtain a negative electrode slurry.
Active material (graphite); 95 parts by mass
Binder (PVdF); 5 parts by mass
Solvent (NMP); 150 parts by mass
The negative electrode slurry was applied to a negative electrode collector of an aluminum foil (thickness 10 μm), followed by drying to form a negative electrode mixture layer on the negative electrode collector. After formation of the negative electrode mixture layer, a coated region (region where the negative electrode mixture layer is formed) except an uncoated region with a size of 10×10 mm as a tab for lead connection was cut to a size of 52×52 mm.
The following substances for a non-aqueous electrolytic solution were mixed to obtain an electrolytic solution.
Additive (fluorinated ethylene carbonate); 3 parts by mass
Non-aqueous electrolytic solution; 97 parts by mass
The non-aqueous electrolytic solution was obtained by dissolving 1 mol/L of LiPF6 as an electrolyte in a mixed solution consisting of ethylene carbonate and dimethylcarbonate at a volume ratio of 1:2 and dissolving 3 parts by mass of fluorinated ethylene carbonate in 97 parts by mass of the resulting solution.
A lithium ion secondary battery according to the embodiment shown in
The positive electrode leads and the negative electrode leads of batteries thus fabricated were connected to the corresponding terminals of a charge and discharge tester (manufactured by Asuka Electronics Co. Ltd.) and constant-voltage constant-current charged at a maximum voltage of 4.2V and a current rate of 2C and constant-current discharged at a current rate 5C up to 2.5V after charge. These processes were repeated 500 cycles. An energy density (Wh/kg) was calculated from the capacity measured during the first discharge and a cycle capacity maintenance ratio (discharge capacity during 500 cycles/discharge capacity during the first cycle×100) was calculated from the capacity after cycles. The capacity maintenance ratio was 92.1%.
A battery was fabricated and tested in the same manner as in Example 1, except that the first active material was used in an amount of 10 parts by mass and the second active material was used in an amount of 80 parts by mass. The capacity maintenance ratio was 90.3%.
A battery was fabricated and tested in the same manner as in Example 1, except that the first active material was used in an amount of 30 parts by mass and the second active material was used in an amount of 60 parts by mass. The capacity maintenance ratio was 95.3%.
A battery was fabricated and tested in the same manner as in Example 1, except that the additive of the electrolytic solution (fluorinated ethylene carbonate) was used in an amount of 0.2 parts by mass and other non-aqueous electrolytic solution was used in an amount of 99.8 parts by mass. The capacity maintenance ratio was 92.4%. The results of Examples 1 to 4 are shown in Table 1.
A battery was fabricated and tested in the same manner as in Example 1, except that the first active material was used in an amount of 85 parts by mass and the second active material was used in an amount of 5 parts by mass. The capacity maintenance ratio was 85.2%. The cycle test results of Comparative Examples are shown in Table 2.
A battery was fabricated and tested in the same manner as in Example 1, except that the additive of the electrolytic solution (fluorinated ethylene carbonate) was used in an amount of 0.1 parts by mass and other non-aqueous electrolytic solution was used in an amount of 99.9 parts by mass. The capacity maintenance ratio was 88.1%.
A battery was fabricated and tested in the same manner as in Example 1, except that the first active material was used in an amount of 90 parts by mass and the second active material was used in an amount of 0 part by mass. The capacity maintenance ratio was 84.8%. The results of Comparative Examples 1 to 3 are shown in Table 2.
Examples 5 to 8 and Comparative Examples 4 to 6 were cases in which the second active material was LiNi0.8Co0.2O2.
A battery was fabricated and tested in the same manner as in Example 1, except that LiNi0.8Co0.2O2 was used as the second active material. The capacity maintenance ratio was 91.3%.
A battery was fabricated and tested in the same manner as in Example 5, except that the first active material was used in an amount of 10 parts by mass and the second active material was used in an amount of 80 parts by mass. The capacity maintenance ratio was 90.6%.
A battery was fabricated and tested in the same manner as in Example 5, except that the first active material was used in an amount of 30 parts by mass and the second active material was used in an amount of 60 parts by mass. The capacity maintenance ratio was 94.8%.
A battery was fabricated and tested in the same manner as in Example 5, except that the additive of the electrolytic solution (fluorinated ethylene carbonate) was used in an amount of 0.2 parts by mass and other non-aqueous electrolytic solution was used in an amount of 99.8 parts by mass. The capacity maintenance ratio was 92.3%. The results of Examples 5 to 8 are shown in Table 3.
A battery was fabricated and tested in the same manner as in Example 5, except that the first active material was used in an amount of 85 parts by mass and the second active material was used in an amount of 5 parts by mass. The capacity maintenance ratio was 86.2%.
A battery was fabricated and tested in the same manner as in Example 5, except that the additive of the electrolytic solution (fluorinated ethylene carbonate) was used in an amount of 0.1 parts by mass and other non-aqueous electrolytic solution was used in an amount of 99.9 parts by mass. The capacity maintenance ratio was 87.9%.
A battery was fabricated and tested in the same manner as in Example 5, except that the first active material was used in an amount of 90 parts by mass and the second active material was used in an amount of 0 part by mass. The capacity maintenance ratio was 85.2%. The results of Comparative Examples 4 to 6 are shown in Table 4.
Examples 9 to 12 and Comparative Examples 7 to 8 were cases in which the second active material was LiNi0.6Co0.2Mn0.2O2.
A battery was fabricated and tested in the same manner as in Example 1, except that the first active material was used in an amount of 75 parts by mass and 15 parts by mass of LiNi0.6Co0.2Mn0.2O2 was used as the second active material. The capacity maintenance ratio was 91.3%.
A battery was fabricated and tested in the same manner as in Example 9, except that the first active material was used in an amount of 5 parts by mass and the second active material was used in an amount of 85 parts by mass. The capacity maintenance ratio was 90.2%.
A battery was fabricated and tested in the same manner as in Example 9, except that the first active material was used in an amount of 25 parts by mass and the second active material was used in an amount of 65 parts by mass. The capacity maintenance ratio was 94.1%.
A battery was fabricated and tested in the same manner as in Example 9, except that the additive of the electrolytic solution (fluorinated ethylene carbonate) was used in an amount of 0.2 parts by mass and other non-aqueous electrolytic solution was used in an amount of 99.8 parts by mass. The capacity maintenance ratio was 91.6%. The results of Examples 9 to 12 are shown in Table 5.
A battery was fabricated and tested in the same manner as in Example 9, except that the first active material was used in an amount of 80 parts by mass and the second active material was used in an amount of 10 parts by mass. The capacity maintenance ratio was 83.8%.
A battery was fabricated and tested in the same manner as in Example 9, except that the additive of the electrolytic solution (fluorinated ethylene carbonate) was used in an amount of 0.1 parts by mass and other non-aqueous electrolytic solution was used in an amount of 99.9 parts by mass. The capacity maintenance ratio was 86.4%. The results of Comparative Examples 7 to 8 are shown in Table 6.
Examples 13 to 15 and Comparative Examples 9 to 10 were cases in which the second active material was LiNi0.3Co0.3Mn0.4O2,
A battery was fabricated and tested in the same manner as in Example 1, except that the first active material was used in an amount of 40 parts by mass and 40 parts by mass of LiNi0.3Co0.3Mn0.4O2 was used as the second active material. The capacity maintenance ratio was 90.6%.
A battery was fabricated and tested in the same manner as in Example 13, except that the first active material was used in an amount of 5 parts by mass and the second active material was used in an amount of 85 parts by mass. The capacity maintenance ratio was 90.0%.
A battery was fabricated and tested in the same manner as in Example 13, except that the additive of the electrolytic solution (fluorinated ethylene carbonate) was used in an amount of 0.2 parts by mass and other non-aqueous electrolytic solution was used in an amount of 99.8 parts by mass. The capacity maintenance ratio was 90.8%. The results of Comparative Examples 13 to 15 are shown in Table 7.
A battery was fabricated and tested in the same manner as in Example 13, except that the first active material was used in an amount of 60 parts by mass and the second active material was used in an amount of 30 parts by mass. The capacity maintenance ratio was 82.1%.
A battery was fabricated in the same manner as in Example 13 and tested, except that the additive of the electrolytic solution (fluorinated ethylene carbonate) was used in an amount of 0.1 parts by mass and other non-aqueous electrolytic solution was used in an amount of 99.9 parts by mass. The capacity maintenance ratio was 84.9%. The results of Comparative Examples 9 to 10 are shown in Table 8.
As can be seen from the test results of Examples 1 to 15, when the content of LiNi0.8Co0.1Mn0.1O2 which was the second active material of the positive electrode active material was 10 to 80 parts by mass (the content of LiNi0.6Co0.2Mn0.2O2 was 15 to 85 parts by mass, and the content of LiNi0.3Co0.3Mn0.4O2 was 50 to 85 parts by mass), good results from cycle tests could be obtained by adjusting the ratio of fluorinated ethylene carbonate (FEC) in the electrolytic solution to 0.2% by mass or higher. In the cycle test, about 90% or higher was considered to be good. In particular, as shown in Example 3, when the content of LiNi0.8Co0.1Mn0.1O2 was 30 parts by mass and the content of fluorinated ethylene carbonate was 3% by mass, particular good results could be obtained. As shown in Comparative Examples 3 and 6, cells having no second active material or fluorinated ethylene carbonate could not exhibit good results. The reason for this was that moisture adsorption caused by coating of the positive electrode active material with conductive carbon was not inhibited due to absence of the fluorinated ethylene carbonate. As shown in Comparative Examples 1, 4, 7 and 9, although fluorinated ethylene carbonate was present in a defined amount of parts by mass, unless the second active material was present in a defined amount of parts by mass, generation of hydrogen fluoride by fluorinated ethylene carbonate and moisture could not be inhibited and good results could not be thus obtained. That is, the amount of nickel contained in the second active material is important and should be 0.3 moles or more with respect to one mole of Li atom. Furthermore, although neither test data in which fluorinated ethylene carbonate exceeds 10% by mass nor test data in which the second active material exceeds the defined amount of parts by mass were disclosed, all of these cases exhibited slightly deteriorated results in the cycle test, as compared to Examples. It is thought that the reason for the former is that, as described above, excess fluorinated ethylene carbonate was present in the cell and the reason for the latter is that excessive nickel affected electric properties of the cell.
Furthermore, the present invention is not limited to the construction of aforementioned embodiments and Examples, but various modifications are possible within the scope of the subject matters of the invention.
In accordance with the above embodiments and examples, a non-aqueous electrolyte secondary battery may include: a first active material of a positive electrode including at least one of carbon-coated LiFePO4, LiMnPO4 and Li3V2(PO4)3; a second active material of the positive electrode including lithium nickel composite oxide; and an electrolytic solution including fluorinated ethylene carbonate. Furthermore, Fe, Mn and V in these formulas may be partially substituted by other element (M). For example, when the metal is Fe, Fe may be partially substituted by other element (M), as represented by Fe1-xMx. When the metal is Mn, Mn may be partially substituted by other element (M), as represented by Mn1-xMx. When the metal is V, V may be partially substituted by other element (M), as represented by V2-yMy. (M) is a metal element and is preferably a transition metal oxide.
Further, in the above embodiments, the formulae of LiFePO4, LiMnPO4 and Li3V2(PO4)3 express crystal structures and basic constituent elements of chemical compounds to be represented by the formulae. Thus, a chemical compound in which a site of Fe, Mn or V is substituted by a different element (having an atomic number of 11 or more) can also be represented by any of the formulae of LiFePO4, LiMnPO4 and Li3V2(PO4)3.
According to the embodiments and examples, a first active material for a positive electrode contains a carbon-coated polyanionic active material, a second active material for the positive electrode contains lithium nickel composite oxide, and an electrolytic solution contains fluorinated ethylene carbonate. As a result, generation of hydrogen fluoride caused by reaction of fluorinated ethylene carbonate with moisture is inhibited by lithium nickel composite oxide used as the second active material. Accordingly, generation of hydrogen fluoride by reaction of fluorinated ethylene carbonate with moisture which has been not solved to date is inhibited and deterioration in cell characteristics is prevented. The absence of deterioration is confirmed by charge/discharge cycle tests.
Furthermore, the non-aqueous electrolyte secondary battery uses carbon-coated polyanion as the first active material for the positive electrode and lithium nickel composite oxide as the second active material of the positive electrode and exhibits high power and superior safety as well as high capacity by mixing a predetermined amount of lithium nickel composite oxide with the positive electrode active material.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2011-216071 | Sep 2011 | JP | national |
