Patent Application
20180076479
The present invention relates to a lithium ion secondary battery, particularly to a lithium ion secondary battery having low moisture content, and further relates to a method of manufacturing a lithium ion secondary battery.
Secondary batteries such as lithium ion secondary batteries have advantages such as high energy density, excellent long-term reliability and the like, and therefore they have been put into practical use in notebook-type personal computers and mobile phones. In recent years, since performance of electronic devices has been improved and its use in electric vehicles and the like has advanced, further improvement of battery characteristics such as safety, higher capacity, longer life, and the like, are strongly demanded.
For example, there have been made various studies on heat-resistant separators for improving the safety of lithium ion secondary batteries. For example, Patent Document 1 discloses a separator for a battery using a porous film composed of an aromatic poly amide represented by a particular formula, in which aromatic rings having para orientation occupy 90 mol % or more of all aromatic rings, the coefficient of static friction μs of 0.3 to 1.8, and Mw/Mn which is the ratio of the weight average molecular weight Mw to the number average molecular weight Mn of the aromatic poly amide is in the range of 1.3 ≦Mw/Mn≦4,6. In addition, Patent Document 2 discloses that in a secondary battery using a positive electrode active material having a particular cumulative particle size distribution and capable of densely packing, by the use of a separator of laminated porous film having the laminate of a heat-resistant layer containing a heat-resistant resin and a shutdown layer containing a thermoplastic resin, the thermal breakdown of the secondary battery can be prevented.
Various studies have also been conducted on active materials, for example, multicomponent lithium transition metal oxides mainly containing nickel as a transition metal have attracted attention as a positive electrode active material that gives high capacity and high energy density.
Furthermore, various electrolyte solution additives such as 1,3-propane sultone described in Patent Document 3 have been studied in order to form a stable film on an electrode to improve battery characteristics.
Meanwhile, moisture contained in a lithium ion secondary battery reacts with a supporting salt such as LiPF6 to generate HF, which deteriorates an electrolyte solution and an active material, so that it may be a cause of impairing the storage characteristics and the cycle characteristics of the lithium ion secondary battery in some cases. In addition, in a lithium ion secondary battery using an electrolyte solution additive such as a sulfonic acid ester compound, the effect of the additive may be impaired by the decomposition of the additive by the generated HF, and the desired sufficient battery characteristics may not be obtained in some cases.
In order to solve such problems, a method of removing adsorbed moisture in an active material by heat treatment, and the like have been studied, as disclosed in a method of manufacturing a negative electrode in Patent Document 4.
However, as described in Patent Document 4, even when moisture adsorbed by the active material itself is removed, there is still a problem that the active material, the binder, the current collector foil, the inner wall of the outer package and the like adsorb moisture during the assembly process of the lithium ion secondary battery, which increases the moisture content in the lithium ion secondary battery. In addition, in order to remove adsorbed moisture (chemically adsorbed water) derived from starting materials of the active material, relatively high temperature condition (120° C. or higher, preferably about 120° C. to 260° C.) is necessary. In conventional manufacturing processes of a secondary battery, however, it is difficult to remove the moisture of this type sufficiently in some cases.
Accordingly, an object of the present invention is to provide a lithium ion secondary battery with a small moisture content, in which adsorbed moisture has been sufficiently removed.
An aspect of the present invention relates to:
a lithium ion secondary battery comprising an electrode element comprising a positive electrode, a negative electrode and a separator, and an electrolyte solution, wherein
the separator has a shrinking ratio of 2% or less by heat treatment at 90° C. for 6 hours, and
a content of physically adsorbed water of the electrode element is 2% by mass or less.
Another aspect of the present invention relates to:
a lithium ion secondary battery comprising an electrode element comprising a positive electrode, a negative electrode and a separator, and an electrolyte solution, wherein
the separator has a shrinking ratio of 2% or less by heat treatment at 90° C. for 6 hours, and
a content of chemically adsorbed water in a positive electrode active material layer of the positive electrode is 1% by mass or less.
Yet another aspect of the present invention relates to:
a method of manufacturing a lithium ion secondary battery comprising an electrode element comprising a positive electrode, a negative electrode and a separator, an electrolyte solution and an outer package, wherein
the separator has a shrinking ratio of 2% or less by heat treatment at 90° C. for 6 hours, and
the method comprises a step of heat-drying the electrode element at 90° C. or higher before injecting the electrolyte solution.
According to the present invention, there is provided a lithium ion secondary battery having a low moisture content.
One embodiment of the present invention relates to a lithium ion secondary battery having low moisture content.
The lithium ion secondary battery according to the first embodiment of the present invention has a separator having a shrinking ratio of 2% or less by heat treatment at 90° C. for 6 hours and has an electrode element having a small moisture content. Here, the electrode element having a low moisture content means an electrode element in which a content of physically adsorbed water per electrode active material layer of the electrode element is 2% by mass or less at least at the time of injecting an electrolyte solution. The content of physically adsorbed water in the electrode element is more preferably 1% by mass or less, and farther more preferably 0.5% by mass or less.
The lithium ion secondary battery according to the second embodiment of the present invention has a separator having a shrinking ratio of 2% or less by heat treatment at 90° C. for 6 hours and a positive electrode active material layer having small moisture content. Here, the positive electrode active material layer having small moisture content means that the content of chemically adsorbed water in the positive electrode active material layer is 3% by mass or less. The content of chemically adsorbed water in the positive electrode active material is more preferably 2% by mass or less, and further preferably 1% by mass or less. Further, in the present embodiment, it is further preferable that the content of the physically adsorbed water of the electrode element is within the range defined in the first embodiment.
In the present specification, the “physically adsorbed water” means moisture due to physical adsorption by adsorption and desorption of water molecules, which can be dehydrated at a relatively low temperature (about 85° C. or higher and less than 120° C.). The content of physically adsorbed water in the electrode element is obtained by cutting the active material layer of the electrode element to be measured quickly to small pieces and measuring the moisture content at 150° C. by the Karl Fischer method.
In the present specification, “chemically adsorbed water” means moisture due to chemical adsorption originated from a starting material or the like of an active material, which requires relatively high temperature (about 120° C. or higher, preferably about 120° C. to about 260° C.) for dehydration. The chemically adsorbed water ratio of the positive electrode active material layer can be measured by the following procedure.
1. The lithium ion secondary battery is disassembled under an environment having a dew point of minus 40° C. or lower, the positive electrode active material layer is taken out and cut finely and kept at 150° C. for 1 hour under a nitrogen atmosphere for preliminary drying to remove the electrolyte solution and physically adsorbed water. Then, the weight (A) (mg) of the positive electrode active material layer is measured.
2. Next, the preliminary dried positive electrode active material layer is maintained at 260° C. for 30 minutes, and the generated water content (B) (mg) is measured by the Karl Fischer coulometric titration method (JIS K 0113).
3. The percentage of chemically adsorbed water that is released by maintaining at 260° C. for 30 minutes (% by mass) is calculated by the following equation.
{Water content (B) (mg) generated from, the positive electrode active material layer after preliminary drying}/{Weight (A) (mg)×100 (% by mass) of the positive electrode active material layer after preliminary drying}
By setting the moisture content of the electrode element and/or the positive electrode active material layer within the above range, the deterioration of the battery due to moisture can be suppressed and battery characteristics such as storage characteristics and cycle characteristics can be improved.
Hereinafter, the configuration of the lithium ion secondary battery according to the present embodiment and examples of each component will be described.
The secondary battery according to the present embodiment can be configured such that an electrode element including a positive electrode, a negative electrode and a separator, and an electrolyte solution are contained in an outer package.
As a separator according to the present embodiment, it is preferable to use a separator having a small heat shrinking ratio. Specifically, it is preferable that the shrinking ratio by heat treatment at 90° C. for 6 hours is 2% or less, more preferably 1% or less, and more preferably 0.5% or less, it is also preferable that it is 0% (it does not shrink).
The heat shrinking ratio of the separator is measured by the following method. A separator is cut into strips of 1 cm width and 10 cm length, and marked at points (2 total points) 1 cm from both ends of the long side, and the distance (A) between the two points before the heat treatment is measured. Next, the separator strips are allowed to stand for 6 hours in a state where substantially no tension is applied in a thermostat oven at 90° C., then cooled to room temperature (eg. 25° C.), and then the distance (B) between the two points is measured. The shrinking ratio of the separator is calculated by.
{A distance (A) between two points before heat treatment−a distance (B) between two points after heat treatment}/a distance (A) between two points before heat treatment×100%
Measurement is performed for five samples in each case of the longitudinal direction and the width direction of the separator to obtain the average value. When the shrinking ratio in the longitudinal direction aim the shrinking ratio in the width direction are different, the larger one is taken as the shrinking ratio in this specification.
By using a separator having a small heat shrinking ratio, the heat resistance of the lithium ion secondary battery can be enhanced. Further, by using a separator having a small shrinking ratio by a heat treatment at 90° C. for 6 hours, even when a manufacturing method including a heat-drying step at 90° C. or higher is adopted as described later, it is possible to prevent deterioration of battery performance due to heat shrinking of the separator.
The material constituting the separator is not particularly limited as long as it satisfies the above-mentioned shrinking ratio, but the material that can be used is, for example, a heat-resistant resin component having a heat melting temperature or thermal decomposition temperature of 160° C. or higher, preferably 180° C. or higher.
Examples of such a heat-resistant resin component include polyethylene terephthalate, cellulose, aramid, polyimide, polyamide, polyphenylene sulfide resin, and the like. Among these, from the viewpoint of heat resistance, cellulose, aramid, polyimide, polyamide, and polyphenylene sulfide resin are preferable. In particular, since heat resistance is 300° C. or higher, heat shrinking is small and shape retention is good, aramid, polyimide, polyamide, polyphenylene sulfide resins are more preferable, and aramid, polyimide, and polyamide resins are further more preferable. In particular, a separator made of an aramid resin can impart excellent heat resistance to the battery, but on the other hand, it has relatively high moisture content and the deterioration of battery characteristics due to moisture may be a problem in some cases. However, with the configuration according to the present embodiment, it is possible to reduce the moisture content of the battery and to suppress deterioration of battery characteristics.
In the present specification, the “heat melting temperature” refers to the temperature measured by differential scanning calorimetry (DSC) according to JIS K 7121, and the “thermal decomposition temperature” refers to the temperature at which the weight decreases by 10% (10% weight loss temperature) when the temperature is raised from 25° C. by rate of 10° C./min in an air flow, and “heat resistance is 300° C. or higher” means that no deformation such as softening is observed at least at 300° C. In the present specification, the phrase “heat melting or thermal decomposition temperature is 160° C. or higher” means that either a heat melting temperature or a thermal decomposition temperature, which is lower, is 160° C. or higher. For example, in the case of a resin which decomposes without melting by heating, it means that the thermal decomposition temperature is 160° C. or higher.
Aramid is an aromatic polyamide in which one or more kinds of aromatic groups are directly linked by amide bond. The aromatic group is, for example, a phenylene group, and two aromatic rings may be bonded by oxygen, sulfur or an alkylene group (for example, a methylene group, an ethylene group, a propylene group or the like). These aromatic groups may have a substituent, and examples of the substituent include an alkyl group (for example, a methyl group, an ethyl group, a propyl group, etc.), an alkoxy group (for example, a methoxy group, an ethoxy group, propoxy group, etc.), halogen (such as chloro group) and the like. The aramid bonds may be either para type or meta type.
Examples of aramids which can be preferably used in the present embodiment include polymetaphenylene isophthalamide, polyparaphenylene terephthalamide, copolyparaphenylene 3,4′-oxydiphenylene terephthalamide, and the like, but not limited to these.
Any structure can be employed as a structure of the separator as long as it has good lithium ion permeability and mechanical strength. For example, a fiber aggregate such as a woven fabric or a nonwoven fabric, and a microporous membrane may be used. Further, it may be a combination of two or more different structures and/or components. Among these, a nonwoven fabric separator tends to cause a self-discharge failure due to a microshort circuit when metallic lithium is formed in a dendrite shape, and therefore a microporous membrane is preferable. In addition, in the case of employing a production method including a heat-drying step at 90° C. or higher described later, it is preferable not to include a polyolefin having a low melting point, and therefore preference is given to, for example, a single layer microporous film of a heat-resistant resin such as an aramid resin.
Further, in one embodiment, it may farther have a layer containing an inorganic tiller such as oxides or nitrides of aluminum, silicon, zirconium, titanium and the like, for example, alumina, boehmite, fine silica particles and the like.
The average pore diameter of the separator in the present embodiment is preferably 0.01 μm or more, more preferably 0.05 μm or more, and further preferably 0.1 μm or more. By having an average pore diameter of 0.1 μm or more, better lithium ion permeability can be maintained. Further, the average pore diameter is preferably 1.5 μm or less, more preferably 1 μm or less, and still more preferably 0.5 μm or less. When the average pore diameter is 1.5 μm or less, it is possible to suppress a short circuit due to precipitation of lithium. From the same viewpoint, it is preferable that the maximum pore diameter of the nonwoven fabric is 5 μm or less. The pore diameter of the nonwoven fabric can be measured by the bubble point method and the mean flow method described in SIM-F-316. Further, the average pore diameter can be taken as an average value of measured values at arbitrary five places of the separator.
Further, in the separator according to this embodiment, the porosity thereof is preferably 40% or more, more preferably 50% or more, and further preferably 60% or more. In addition, it Is preferably 90% or less, and more preferably 80% or less. When the porosity is within the above range, sufficient mechanical strength and good rate property can be obtained. The porosity of the separator may be determined by measuring the bulk density according to JIS P 8118, and calculated according to the equation:
Porosity (%)=[1−(bulk density p (g/cms)/theoretical density of material p0 (g/cm3))]×100
As the other measurement methods, a direct observation method using an electron microscope and a mercury penetration method using a mercury porosimeter are exemplified.
Although the thickness of the separator in this embodiment is not particularly limited, it Is generally preferably 8 μm or more and 30 μm or less, more preferably 9 μm or more and 27 μm or less, and still more preferably 10 μm or more and 25 μm or less. When the thickness of the separator is 10 μm or more, the safety of the secondary battery can be further enhanced. When the thickness of the separator is 25 μm or less, it is possible to maintain a favorable charge/discharge rate.
The positive electrode according to the present embodiment comprises a positive electrode current collector and a positive electrode active material layer formed on one side or both sides of the positive electrode current collector.
The positive electrode active material is not particularly limited as long as it can absorb and desorb lithium, and known positive electrode active materials can be used.
From the viewpoint of high energy density, a compound having high capacity is preferably contained. Examples of the high capacity compound include lithium nickelate (LiNiO2), or lithium nickel composite oxides in which a part of the Ni of lithium nickelate is replaced by another metal element, and layered lithium nickel composite oxides represented by the following formula (A) are preferred.
LiyNi(i-x)MxO2 (A)
wherein 0≦×<1, 0<y≦1.5, and M is at least one element selected from the group consisting of Co, Al, Mm, Fe, Mg, Ba, Ti and B.
As one embodiment of the positive electrode active material, it is preferred that in the formula (A), 0≦×<1, 0<y≦1.2, and M is at least one element selected from the group consisting of Co, Al, Ms, Fe, Ti, and B.
From the viewpoint of high capacity, it is preferable that the Ni content is high, that is, so-called high-nickel lithium nickel composite oxides are preferably contained. Such a compound has a high capacity because it has a high Ni content, and has a longer lifetime as compared with LiNiO2 because a part of Ni is substituted. As one embodiment of the high-nickel lithium, nickel composite oxide, a compound, represented by the following formula (1) is exemplified.
LiαNiβMeγO2 (1)
wherein 0.9≦α≦1.5, β+γ=1, 0.5≦β<1, Me is at least one selected from the group consisting of Co, Mn, Al, Fe, Mg, Ba, Ti, and B.
In formula (1), α is more preferably 1≦α≦1.2. β is more preferably β≧0.6, further more preferably β≧0.7, and particularly preferably β≧0.8. Further, Me preferably comprises at least one selected from. Cos Mn, Al, and Fe, and more preferably comprises at least one selected from Co, Mn and Al.
Examples of the compound represented by the formula (1) include LiαNiβCoγMδO2 (0<α≦1.2, preferably 1≦α≦1.2, β+γ+δ=1, β≧0.7, and γ≦0.2) (may be abbreviated as NCM), and LiαNiβCoγAlδO2 (0<α≦1.5, preferably 1≦α≦1.5, and more preferably 1≦α≦1.2, β+γ+δ=1, β≧0.6, preferably β≧0.7, and γ≦0.2) (may be abbreviated as NCA)), and particularly preferably LiαNiβCoγMnδO2 (1≦α≦1.2, β+γ+δ=1, β≧0.8, γ≦0.2) or LiNiβCoγMn67 O2 (0.75 23 α≦0.85, 0.05 ≦γ≦0.15, and 0.10≦δ≦0.20). More specifically, for example, LiNi0.8Mn0.15Co0.05O2, LiNi0.8Co0.1Mn0.1O2, LiNi0.8Co0.15Al0.05O2, and LiNi0.3Co0.1Al0.1O2 may be preferably used.
The above high-nickel lithium nickel composite oxide may be used alone or in combination of two or more. From the viewpoint of increasing the capacity. It Is preferable that the above high-nickel lithium nickel composite oxide is contained in an amount of preferably 75% by mass or more, more preferably 85% by mass or more, still more preferably 90% by mass or more, and still more particularly preferably 95% by mass or more. Also, 100% by mass may be preferable.
From the viewpoint of thermal stability, it is also preferred that the content of Ni does not exceed 0.5, that is, x is 0.5 or more in the formula (A). It is more preferable that 1<y≦1.2 In formula (A). In addition, it Is also preferred that particular transition metals do not exceed half. Examples of such compounds include LiαNiβCoγMnδO2 (0<α≦1.2, preferably 1≦α≦1.2, β+γ+δ=1, 0.2 ≦β≦0.5, 0.1≦γ≦0.4, and 0.1≦δ≦0.4). More specific examples may include LiNi0.4Co0.3Mn0.3O2 (abbreviated as NCM433), LiNi1/3Co1/3Mn1/3O2, LiNi0.5Co0.2Mn0.3O2 (abbreviated as NCM523), and LiNi0.5Co0.3Mn0.2O2 (abbreviated as NCM532) (also including these in which the content of each transition metal fluctuates by about 10% in these compounds).
In addition, two or more compounds represented by the formula (A) may be mixed and used, and, for example, it is also preferred that NCM532 or NCM523 and NCM433 are mixed in the range of 9:1 to 1:9 (as a typical example, 2:1) and used. Further, by mixing a material in which the content of Ni is high (α is 0.6 or more) in the formula (1) and a material in which the content of Ni does not exceed 0.5 (β is 0.5 or less, for example, NCM433), a battery having high capacity and high thermal stability can also be formed.
Examples of the positive electrode active materials other than the above include lithium manganate having a layered structure or a spinel structure such as LiMnO2, LixMn2O4 (0<x<2), Li2MnO3, and LixMn1.5Ni0.5O4 (0<x<2); LiCoO2 or materials in which a part of the transition metal in this material is replaced by other metal(s); materials in which Li is excessive as compared with the stoichiometric composition in these lithium transition metal oxides; materials having olivine structure such as LiMPO4, and the like. In addition, materials in which a part of elements in these metal oxides is substituted by Al, Fe, P, Ti, Si, Pb, Sn, In, Bi, Ag, Ba, Ca, Hg, Pd, Pt, Te, Zn, La are also usable.
Any of the positive electrode active materials described above may be used alone or in combination of two or more,
The median particle diameter of the positive electrode active material is preferably 0.01 to 50 μm, and further more preferably 0.02 to 40 μm. When, the particle size is 0.02 μm or more, the elution of constituent elements of the positive electrode active material can be further suppressed and deterioration due to contact with the electrolyte solution can be further suppressed. In addition, when the particle size is 50 μm or less, insertion and release of lithium ions is facilitated smoothly, and electric resistance can be further reduced. The median particle diameter is a 50% cumulative diameter D50 and can be measured by a laser diffraction scattering type particle size distribution measuring apparatus.
The specific surface area of the positive electrode active material is, for example, 0.01 to 5 m2/g, preferably 0,05 to 0.4 m2/g, more preferably 0,1 to 3 m2/g, and more preferably 2 to 2 m2/g. When the specific surface area is within such a range, it is possible to adjust the contact area with the electrolyte solution within an appropriate range. In other words, by setting the specific surface area to 0.01 m2/g or more, absorption and desorption of lithium ions is facilitated smoothly, and the resistance can be further reduced. Further, when the specific surface area is 5 m2/g or less, it is possible to further suppress the progress of the decomposition of the electrolyte solution and the elution of constituent elements of the active material. The specific surface area can be measured by usual BET specific surface area measurement method. Further, according to one embodiment of the present invention, positive electrode active materials having a BET specific surface area of 0.5 to 2.5 m2/g can also be preferably used.
Further, the above lithium transition metal compounds may be composed, of primary particles, secondary particles formed by the aggregation, of primary particles, or a mixture of primary particles and secondary particles.
In general, the above lithium transition metal compounds may be prepared by mixing Li raw materials such as LiOH, LiHCO3, Li2CO3, Li2O, Li2SO4 and the like; Ni raw materials such as NiO, Ni(OH)2, NiSO4, Ni(NO3) and the like; and oxides, carbonates, hydroxides, sulfides and the like of the respective substituting elements so as to have a target metal composition ratio, and calcining the mixture in air or oxygen.
Examples of the positive electrode binder include, but not particularly limited to, for example, polyvinylidene fluoride, vinylidene fluoride-hexafluoropropylene copolymer, vinylidene fluoride-tetrafluoroethylene copolymer, styrene-butadiene copolymer rubber (SBR), polytetrafluoroethylene, polypropylene, polyethylene, polyimide, polyamideimide, polyacrylic acid and the like. Among them, polyvinylidene fluoride or polytetrafluoroethylene is preferable from the viewpoint of versatility and low cost, and polyvinylidene fluoride is more preferable. The amount of the positive electrode binder is preferably 2 to 10 parts by mass based on 100 parts by mass of the positive electrode active material, from the viewpoint of the binding strength and energy density that are in a trade-off relation with each other.
For the coating layer containing the positive electrode active material, a conductive assisting agent may be added for the purpose of lowering the impedance. Examples of the conductive assisting agent include, flake-dike, soot, and fibrous carbon fine particles and the like, for example, graphite, carbon black, acetylene black, vapor grown carbon fibers and the like. The content of the conductive assisting agent for the positive electrode is preferably 1 to 5 parts by mass with respect to 100 parts by mass of the positive electrode active material.
The positive electrode current collector is not particularly limited, but for example, a current collector using aluminum, an aluminum alloy, iron-nickel-chromium-molybdenum based stainless steel can be used.
The positive electrode according to the present embodiment can be produced by a known method. For example, a slurry containing a positive electrode active material, a binder and, if necessary, a conductive assisting agent and the like and a dispersion medium is applied on a current collector, dried to remove the dispersion medium, and then pressed to form a positive electrode. The positive electrode active material layer is formed so that the current collector has an extension portion to be connected to a positive electrode terminal. That is, the positive electrode active material layer is not coated on this extension portion.
The negative electrode according to the present embodiment comprises a negative electrode current collector and a negative electrode active material layer formed on one side or both sides of the negative electrode current collector.
The negative electrode active material in the present embodiment is not particularly limited, and examples thereof include carbon materials capable of absorbing and desorbing lithium ions, metals capable of forming an alloy with lithium, a metal oxide capable of absorbing and desorbing lithium ions, and the like.
Examples of the carbon material include graphite (natural graphite, artificial graphite, etc.), amorphous carbon, diamond-like carbon, carbon nanotube, or composites of these. Highly crystalline graphite has high electrical conductivity and is excellent in adhesion to a negative electrode current collector made of a metal such as copper and in voltage flatness. On the other hand, amorphous carbons having a low crystallinity exhibit relatively small volume expansion, and therefore halve effect of highly relaxing the volume expansion of the whole negative electrode, and hardly undergo the degradation due to nonuniformity such as crystal grain boundaries and defects.
Examples of metals include Al, Si, Pb, Sn, In, Bi, Ag, Ba, Ca, Hg, Pd, Pt, Te, Zn, La, and alloys of two or more of these. These metals or alloys may be used, in combination of two or more. In addition, these metals or alloys may contain, one or more nonmetallic elements.
Examples of the metal oxide include silicon oxide, aluminum oxide, tin oxide, indium oxide, zinc oxide, lithium oxide, and composites of these. It is preferable to include tin oxide or silicon oxide, and more preferably silicon oxide, as a negative electrode active material. This is because silicon oxide is relatively stable and hardly causes reaction with other compounds. It is also preferable that all or a part thereof has an amorphous structure. Further, the amorphous structure is considered to have relatively few nonuniformity-associated elements, such as crystal grain boundaries and defects. The fact that all or a part of the metal oxide has an amorphous structure can be confirmed by X-ray diffraction measurement (general XED measurement). Specifically, when the metal oxide does not have an amorphous structure, a peak characteristic to the metal oxide is observed, but in the case where all or a part of the metal oxide has an amorphous structure, a peak characteristic to metal oxide is observed as a broad peak.
Carbon materials, metals, and metal oxides may be not only used alone, but also in combination. For example, similar materials such as graphite and amorphous carbon may be mixed with each other, or different materials such as graphite and silicon may be mixed. In one embodiment, from the viewpoint of high energy density, in addition to carbon materials such as graphite. It is also preferable to contain 0.01 to 20% by mass of metal Si and/or SiOx (0<x>2).
The form of the negative electrode active material is not particularly limited, but particulate ones can be used. The average particle diameter of the negative electrode active material is preferably 0.1 μm or more and 20 μm. or less, more preferably 0.5 μm or more and 15 μm or less, and further preferably 1 μm or more and 10 μm or less. Here, the average particle size is 50% cumulative diameter D50 (median diameter), and it is obtained by particle size distribution measurement by laser diffraction scattering method. If the average particle diameter of the negative electrode active material is too small, the falling of powder increases, deteriorating cycle characteristics in some eases. In addition, if the average particle diameter is too large, movement of lithium ions may be inhibited in some cases.
The specific surface area of the negative electrode active material is preferably 0.2 m2/g or more, more preferably 1.0 m2/g or more, still more preferably 2.0 m2/g or more, whereas it is preferably 9.0 m2/g or less, more preferably 8.0 m2/g or less, and even more preferably 7.0 m2/g or less. The specific surface area can be measured by usual BET specific surface area measurement method. Furthermore, according to one embodiment of the present invention, negative electrode active materials having a BET specific surface area of 1 to 10 m2/g can also be preferably used.
Examples of the negative electrode binder include polyvinylidene fluoride, vinylidene fluoride-hexafluoropropylene copolymer, vinylidene fluoride-tetrafluoroethylene copolymer, styrene-butadiene copolymer rubber, polytetrafluoroethylene, polypropylene, polyethylene, polyimide, polyamideimide, polyacrylic acid and the like. Among them, polyvinylidene fluoride or polytetrafluoroethylene is preferable from the viewpoint of versatility and low cost, and polyvinylidene fluoride is more preferable. It is also possible to mix a styrene-butadiene copolymer rubber and carboxymethyl cellulose to prepare a binder. The amount of the negative electrode binder is preferably 1 to 20 parts by mass based on 100 parts by mass of the negative electrode active material, from the viewpoint of the binding strength and energy density being in a trade-off relation with each other.
For the coating layer containing the negative electrode active material, a conductive assisting agent may be added for the purpose of lowering the impedance. Examples of the conductive assisting agent include, flake-like, soot, and fibrous carbon fine particles and the like, for example, carbon black, acetylene black, vapor grown carbon fibers and the like. The content of the conductive assisting agent is preferably 0.3 to 5 parts by mass with respect to 100 parts by mass of the negative electrode active material.
As the negative electrode current collector, from the view point of electrochemical stability, aluminum, nickel, stainless steel, chromium, copper, silver, and alloys thereof are preferred. As the shape thereof, foil, flat plate, mesh and the like are exemplified. In particular, copper or an alloy of copper is preferable.
The negative electrode according to the present embodiment can be produced by a known method. For example, a slurry containing a negative electrode active material, a binder and, if necessary, a conductive assisting agent and the like and a dispersion medium is applied on a current collector so that the coating amount after drying fells within a desired range, dried to remove the dispersion medium, and then pressed to form a negative electrode. The negative electrode active material layer is formed so that the current collector has an extension portion to be connected to a negative electrode terminal. That is, the negative electrode active material layer is not coated on this extension portion.
As the electrolyte solution of the secondary battery according to the present embodiment, a nonaqueous electrolyte solution containing a nonaqueous solvent and a supporting salt that is stable at the operating potential of the battery is preferable.
Examples of nonaqueous solvents include aprotic organic solvents, for examples, cyclic carbonates such as propylene carbonate (PC), ethylene carbonate (EC) and butylene carbonate (BC); open-chain carbonates such as dimethyl carbonate (DMC), diethyl carbonate (DEC), ethyl methyl carbonate (EMC) and dipropyl carbonate (DPC); aliphatic carboxylic acid esters such as propylene carbonate derivatives, methyl formate, methyl acetate and ethyl propionate; ethers such as diethyl ether and ethyl propyl ether; phosphoric acid esters such as trimethyl phosphate, triethyl phosphate, tripropyl phosphate, trioctyl phosphate and triphenyl phosphate; and fluorinated aprotic organic solvents obtainable by substituting at least a part of the hydrogen atoms of these compounds with fluorine atom(s), and the like.
Among them, cyclic or open-chain carbonate(s) such as ethylene carbonate (EC), propylene carbonate (PC), butylene carbonate (BC), dimethyl carbonate (DMC), diethyl carbonate (DEC), ethyl methyl carbonate (MEC), dipropyl carbonate (DPC) and the like is preferably contained.
Nonaqueous solvent may be used, alone, or in combination of two or more.
As the supporting salt, for example, lithium salts can be used. Examples of lithium salts include LiPF6, lithium imide salts, LiAsF6, LiAlCl4, LIClO4, LiBF4, LiSbF6 and the like. As lithium imide salt, LiN(CkF2k+1SO2) (wherein k and m are each independently a natural number, preferably 1 or 2) is exemplified. These may be used alone or in combination of two or more of these. From the viewpoint of cost reduction, LiPF6 is preferable.
The concentration of the lithium salt in the electrolyte solution is preferably 0.7 mol/L or more and 2.0 mol/L or less. When the concentration of the lithium salt is 0.7 mol/L or more, sufficient ionic conductivity can be obtained. Also, when the concentration of the lithium salt is 2.0 mol/L or less, the viscosity can be lowered and movement of lithium ions is not disturbed.
The electrolyte solution according to the present embodiment may further contain additives. The additive is not particularly limited, and examples thereof include film forming additives, overcharge inhibitors, surfactants, and the like.
Among these, preferred, additives in the present embodiment include sulfonic acid ester compounds and the like. Specific examples of the sulfonic acid ester compound include cyclic monosulfonic acid ester compounds, cyclic disulfonic acid ester compounds, open-chain sulfonic acid ester compounds, and the like.
These additives can form a film on the electrode as the secondary battery is charged and discharged, which suppresses the decomposition of the electrolyte solution and supporting salt, whereby improving the lifetime characteristics of the battery. On the other hand, these additives are easily decomposed when water content in the battery is high because hydrogen ions generated by the reaction of moisture and a supporting salt act on ester bonds, and the effect of the additive cannot be obtained in some cases. However, in the lithium ion secondary battery having a low moisture content according to the present embodiment, the decomposition of the additive due to moisture is suppressed and a film is formed more effectively, and thus the excellent effect of extending a life time can be obtained.
Examples of cyclic monosulfonic acid ester compounds include, for example, compounds represented by the following formula (2).
(In the formula (2), n is an integer of 0 or more and 2 or less. R5 to R10, independently one another, represent a hydrogen atom, a substituted or unsubstituted alkyl group having 1 to 12 carbon atoms, a substituted or unsubstituted fluoroalkyl group having 1 to 6 carbon atoms, a polyfluoroalkyl group having 1 to 6 carbon atoms.)
In the compound represented by the formula (2), n is preferably 0 or 1, and R5 to R10, independently one another, represent a hydrogen atom, a substituted or unsubstituted alkyl group having 1 to 12 carbon atoms, a polyfluoroalkyl group having 1 to 5 carbon atoms, and more preferably, independently one another, represent a hydrogen atom or a polyfluoroalkyl group having 1 to 5 carbon atoms. More preferably, all of R5 to R10 are hydrogen atoms, or one or two of R5 to R10 is a polyfluoroalkyl group having 1to 5 carbon atoms and the others are hydrogen atoms. The above-mentioned polyfluoroalkyl group having 1 to 5 carbon atoms is preferably a trifiuoromethyl group.
Examples of cyclic monosulfonic acid ester compounds include 1,3-propane sultone, 1,2-propane sultone, 1,4-butane sultone, 1,2-butane sultone, 1,3-butane sultone, 2,4-butane sultone, 1,8-pentane sultone and the like.
Examples of cyclic disulfonic acid ester compounds include compound represented by the following formula (3).
In the formula (3), R1 and R2 are each independently represents a substituent selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 5 carbon atoms, a halogen group, and an amino group. R3 represents an alkylene group having 1 to 5 carbon atoms, a carbonyl group, a sulfonyl group, a fluoroalkylene group having 1 to 6 carbon atoms, or a divalent group having 2 to 6 carbon atoms in which alkylene units or fluoroalkylene units are bonded via an ether group.
In the formula (3), R1 and R2 are each independently preferably a hydrogen atom, an alkyl group having 1 to 3 carbon atoms or a halogen group, and R3 is more preferably an alkylene group or fluoroalkylene group having 1or 2 carbon atoms.
Preferable examples of the cyclic disulfonic acid, ester represented by the formula (3) include, but are not limited to, the following compounds.
As the open-chain chain disulfonic acid ester, for example, open-chain disulfonic acid esters represented by the following formula (4) can be exemplified.
In the formula (4), R4 and R7, independently each other, represent an atom or a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 5 carbon atoms, an alkoxy group having 1 to 5 carbon atoms, an fluoroalkyl group having 1 to 5 carbon atoms, an polyfluoroalkyl group having 1 to 5 carbon atoms, —SO2X3 (X3 is an alkyl group having 1 to 5carbon atoms), —SY1 (Y1 is an alkyl group having 1 to 5 carbon atoms), —COZ (Z is a hydrogen atom or an alkyl group having 1 to 5 carbon atoms), and a halogen atom, R5 and R6, independently each other, represent an alkyl group having 1 to 5 carbon atoms, an alkoxy group having 1 to 5 carbon atoms, a phenoxy group, a fluoroalkyl group having 1 to 5 carbon atoms, a polyfluoroalkyl group having 1 to 5 carbon atoms, a fluoroalkoxy group having 1 to 5 carbon atoms, a polyfluoroalkoxy group having 1 to 5 carbon atoms, a hydroxyl group, a halogen atom, —NX4X5 (X4 and X5 independently each other represent a hydrogen atom, or an alkyl group having 1 to 5 carbon atoms) and —NY2CONY3Y4 (Y2 to Y4, independently each other, represent a hydrogen atom or an alkyl group having 1 to 5 carbon atoms).
In the formula (4), R4 and R7 are, independently each other, preferably a hydrogen atom, an alkyl group having 1 or 2 carbon atoms, a fluoroalkyl group having 1 or 2 carbon atoms, or a halogen atom, and R5 and R6, independently each other, represent an alkyl group having 1 to 3 carbon atoms, an alkoxy group having 1 to 8 carbon atoms, a fluoroalkyl group having 1 to 3 carbon atoms, a hydroxyl group or a halogen atom.
Examples of the open-chain disulfonic acid ester compound represented by the formula (4) include, but not limited to, the following compounds.
Particularly preferred compounds of the open-chain disulfonic acid ester compound represented by the formula (4) include, for example, compounds in which R4 and R7 are hydrogen atoms and R6 and R6 are methoxy groups (Compound (101)), but it is not limited thereto.
Among them, the sulfonic acid ester compound used in the present embodiment is preferably cyclic monosulfonic acid ester compounds such as 1,3-propane sultone, 1,4-butane sultone or the like, and cyclic disulfonic acid ester compounds such as methylene methane disulfonic acid ester compound (compound (3-1)).
The content of the sulfur-based additive is preferably in the range of 0.005% by mass to 10% by mass and more preferably from 0.01% by mass to 5% by mass. When it is contained in an amount of 0.005% by mass, or more a sufficient film effect can be obtained. When the content is 10% by mass or less, it is possible to suppress an increase in the viscosity of the electrolyte solution and an increase in resistance accompanied thereby.
The sulfur-based additives may be used alone or in combination of two or more.
An outer package can be appropriately selected as long as it has stability in an electrolyte solution and sufficient steam barrier properties. For example, in the case of a stacked laminate type secondary battery, laminate films, such as polypropylene, polyethylene or the like coated with aluminium, silica or alumina can be used as the outer package. Examples of the outer package other than the film include a metal (stainless steel, aluminum etc.) case and a resin case. The outer package may be constituted by a single member or may be constituted by combining a plurality of members. In one embodiment, it is preferable to use an aluminum laminate film from the viewpoints of weight reduction, heat dissipation and easiness of processability. In another embodiment, it is preferable to use a metallic outer package from the viewpoint that a higher temperature condition can be employed in the heat-drying step in the manufacturing method according to the present invention.
Secondary batteries may be selected from, depending on a structure of electrode or a shape, various types such as cylindrical type, flat spirally wound prismatic type, laminated square shape type, coin type, flat wound, laminated type and stacked laminate type and the like. Although the present invention can be applied to any type of secondary battery, the stacked laminate type is preferable in that it is inexpensive and has excellent flexibility in designing the cell capacity by changing the number of stacked electrodes.
Examples of the laminate resin film used for the laminate type include aluminum, aluminum alloy and titanium foil, and the like. Examples of the material of the heat bonding portion of the metal laminate resin film include thermoplastic polymer materials such as polyethylene, polypropylene, polyethylene terephthalate and the like. In addition, each of the metal laminate resin layer and the metal foil layer is not limited to one layer, and may be two or more layers.
As another embodiment, a secondary battery having a structure as shown in
In the battery element 20, a plurality of positive electrodes 30 and a plurality of negative electrodes 40 are alternately stacked with separators 25 sandwiched therebetween as shown in
In the secondary battery in
The film package 10 is composed of two films 10-1 and 10-2 in this example. The films 10-1 and 10-2 are heat-sealed to each other in the peripheral portion of the battery element 20 and hermetically sealed. In
Of course, the electrode tabs may be drawn out from different two sides respectively. In addition, regarding the arrangement of the films, in
By adopting a configuration with small water content in the electrode element and/or the positive electrode active material layer according to the present embodiment, high effect of improving battery characteristic can be obtained, particularly when “an electrode that easily adsorbs moisture” as exemplified below is used.
Such a positive electrode active material contains chemically adsorbed water derived from an impurity of a raw material origin, which may become a cause of increase in moisture content of the lithium ion secondary battery.
Since such positive electrode active materials are easily broken when forming a positive electrode active material layer, they re-adsorb a large amount of moisture, which may become a cause of increase in moisture content of the lithium ion secondary battery.
Since these materials have a high moisture adsorption rate, they re-adsorb a large amount of moisture, which may become a cause of increase in moisture content of the lithium ion secondary battery.
As a lithium ion secondary battery according to the present embodiment, by adopting a configuration in which the moisture content of the electrode element and/or the positive electrode active material layer is small, the moisture content of the lithium ion secondary battery can be certainly reduced even when the above-described electrode which easily adsorbs moisture is used.
The lithium ion secondary battery according to the present embodiment can be produced, for example, by the following manufacturing method.
A further embodiment of the present invention relates to a method for producing a lithium ion secondary battery having a low moisture content.
An example of a method for manufacturing a lithium ion secondary battery will be described taking a stacked type lithium ion secondary battery as an example. First, in the dry air or an inert atmosphere, the positive electrode and the negative electrode are placed to oppose to each other via a separator to form an electrode element. Next, this electrode element is housed in an outer package, and then an electrolyte solution is injected to impregnate the electrode with the electrolyte solution. Then, the opening of the package is sealed to complete a secondary battery. Here, the method of manufacturing a lithium, ion secondary battery according to the present embodiment is characterized in that:
In the manufacturing method according to the present embodiment, by using a separator having a shrinking ratio of 2% or less by heat treatment at 90° C. for 6 hours, it is possible to perform heat-drying treatment to a semi-finished product of the lithium ion secondary battery, namely to a product of the state in which at least an electrode element has been formed. Therefore, it is possible to promptly inject the electrolyte solution after removing moisture by heat-drying. Therefore, re-adsorption of moisture during the assembly process of the secondary battery can be sufficiently suppressed. Furthermore, by using a highly heat resistant separator, it is possible to perform heat-drying of the electrode element at a higher temperature. As a result, in addition to the physically adsorbed, water, the chemically adsorbed water can be removed. As a result, it is possible to manufacture a lithium ion secondary battery having a lower moisture content, in which deterioration in battery characteristics due to moisture is suppressed.
In one embodiment, from the viewpoint of water removal efficiency, it is preferable to set the temperature condition in the step of performing heat-drying to 100° C. or higher. Further, from the viewpoint of removal efficiency of chemically adsorbed water, it is preferable to perform at 120° C. or higher, and more preferably 180° C. or higher. The upper limit of the temperature condition can be selected considering the heat resistance of the constituent members of the lithium ion secondary battery to be subjected to the heat-drying step, but it is generally 220° C. or lower, and if a laminate film outer package is used, it is preferably 160° C. or lower in general. Herein, the temperature of heat-drying can be appropriately selected in consideration of the material of the outer package, the manufacturing environment (humidity condition), and the like as described later.
The time for performing the heat-drying can be appropriately determined depending on combination, with the temperature condition or the like, but it is preferably, for example, 20 minutes or more, and preferably 6hours or more. From the viewpoint of production efficiency, it is preferably 24 hours or less.
It is preferable to perform the heat-drying in an inert gas such as nitrogen. From the viewpoint of water removal efficiency, it is preferably carried out under reduced pressure of 0.1 or less.
Hereinafter, embodiments of the manufacturing method according to the present invention will be exemplified, but the present invention is not limited to these embodiments.
A method of manufacturing a lithium ion secondary battery according to the present embodiment comprises the steps of:
preparing an electrode element having a positive electrode, a negative electrode and a separator;
accommodating the produced electrode element in a laminate outer package;
heat-drying the laminate outer package and the electrode element accommodated in the laminate outer package at 90° C. or higher and 160° C. or lower, for example 90° C. or higher and 100° C. or lower; and
then, injecting an electrolyte solution and sealing the laminated outer package.
According to Embodiment 1, since the high-temperature drying step is performed in a state where the electrode element is accommodated in the outer package, the high-temperature drying condition can be maintained until immediately before the injection of the electrolyte solution, and the adsorption of moisture after the high-temperature drying step can be suppressed.
A method of manufacturing a lithium ion secondary battery according to the present embodiment comprises the steps of:
preparing an electrode element having a positive electrode, a negative electrode and a separator;
heat-drying the prepared electrode element at 90° C. or higher and 160° C. or lower;
accommodating the heat-dried electrode element in an outer package; and
then, injecting an electrolyte solution and sealing the outer package.
According to the second embodiment, since the heating temperature can be set without considering the heat resistant temperature of the outer package, it is possible to perform a high temperature drying step of the electrode element, for example, at a high temperature not lower than the heat resistant temperature of the outer package, and therefore, the removal of moisture of the electrode element can be effectively performed within a short time. Therefore, it can be preferably applied to the production of a lithium ion secondary battery even using a laminate outer package having a relatively low heat resistance. In one embodiment, it is also preferable to perform the step of heat-drying at 120° C. or higher, more preferably 130° C. or higher. In the present embodiment, the process from the step of heat-drying the electrode element to the step of injecting the electrolyte solution is preferably performed in an environment of low humidity (preferably 0.6 RH % or less). This makes it possible to further suppress re-absorption of moisture in the electrode element in the step of laminate coating.
A method of manufacturing a lithium ion secondary battery according to the present embodiment comprises the steps of:
preparing an electrode element having a positive electrode, a negative electrode and a separator;
accommodating the produced electrode element in a metal outer package;
drying at high temperature the metal outer package and the electrode element accommodated in the metal outer package at 90° C. or higher, preferably 150° C. or higher and 220° C. or lower; and
then, injecting an electrolyte solution and sealing the metal outer package.
According to Embodiment 3, since the metal outer package is used, it is possible to perform the high-temperature drying process at a higher temperature condition, and therefore chemically adsorbed water in addition to the physically adsorbed water can be removed more effectively. In addition, from the viewpoint of removal efficiency of chemically adsorbed water, the temperature may be preferably set in some cases at 160° C. or higher, and more preferably 200° C. or higher. In addition, since the high-temperature drying step is performed in a state where the electrode element is accommodated in the outer package, the high-temperature drying condition can be maintained until immediately before the injection of the electrolyte solution, and the adsorption of moisture after the high-temperature drying step can be further suppressed.
The configuration, of the lithium ion secondary battery that can be produced by the manufacturing method according to the present embodiment is not particularly limited as long as it is a secondary battery using a separator having a shrinking ratio of 2% or less by heat treatment at 90° for 6 hours. For example, the constituent elements detailed above in this specification can be appropriately selected and used for the lithium ion secondary battery.
Hereinafter, examples of preferred embodiments of the present invention will be described.
A plurality of secondary batteries according to the present embodiment may be combined to form an assembled battery. The assembled battery may be configured, by connecting two or more secondary batteries according to the present embodiment in series or in parallel or in combination of both. The connection in series and/or parallel makes it possible to adjust the capacitance and voltage freely. The number of secondary batteries included in the assembled battery can be set appropriately according to the battery capacity and output.
The secondary battery or the assembled battery according to the present embodiment can be used in vehicles. Vehicles according to an embodiment of the present invention include hybrid vehicles, fuel cell vehicles, electric vehicles (besides four-wheel vehicles (cars, trucks, commercial vehicles such, as buses, light automobiles, etc.) two-wheeled vehicle (bike) and tricycle), and the like. The vehicles according to the present embodiment is not limited to automobiles, it may be a variety of power source of other vehicles, such as a moving body like a train.
The secondary battery or the assembled battery according to the present embodiment can be used in power storage system. The power storage systems according to the present embodiment include, for example, those which is connected between the commercial power supply and loads of household, appliances and used as a backup power source or an auxiliary power in the event of power outage or the like, or those used as a large scale power storage that stabilize power output with large time variation supplied by renewable energy, for example, solar power generation.
Hereinafter, the present invention will be described in detail with reference to examples, but the present invention is not limited to these examples.
LiNi0.6Mn0.15Co0.05O2 as a positive electrode active material, PVdF as a binder and acetylene black as a conductive assisting agent were mixed at a weight ratio of 92/4/4 and kneaded using N-methylpyrrolidone as a solvent to prepare a positive electrode slurry. The prepared slurry was applied to one side of an aluminum foil current collector having a thickness of 20 μm, dried, and further pressed to obtain a positive electrode.
Artificial graphite as a negative electrode active material, PVdF as a binder and acetylene black as a conductive assisting agent were mixed at a weight ratio of 98/5/2 and kneaded using N-methylpyrrolidone as a solvent to prepare a negative electrode slurry. The prepared slurry was applied on one side of a copper foil current collector having a thickness of 20 μm, heat treated at 80° C. in a nitrogen, atmosphere, dried, and further pressed to obtain a negative electrode.
Three prepared positive electrodes and four negative electrodes were stacked via aramid micropore us membranes (shrinking ratio of 0.5% at 90° C. for 6 hours). End portions of the positive electrode current collectors on which the positive electrode active material was not formed and end portions of the negative electrode current collectors on which the negative electrode active material was not formed were respectively welded. To the respective welded portions, a positive electrode terminal formed of aluminum and a negative electrode terminal formed of nickel were further welded respectively to obtain an electrode element having a planar stacked structure.
LiPF6 as a supporting electrolyte was dissolved in a mixed solvent of EC/DEC (volume ratio: EC/DEC=30/70) as nonaqueous solvent so as to have a concentration of 1 M in an electrolyte solution. Further, methylene methane disulfonic acid ester (compound (3-1)) as an additive was dissolved in the electrolyte solution so as to have a concentration of 1% by mass, to obtain an electrolyte solution.
The prepared electrode element was accommodated in an aluminum laminate outer package and heat-dried in a dry nitrogen atmosphere while maintaining the temperature condition at 90 to 100° C. for 6 hours. Next, the electrolyte solution was quickly injected, and the outer package was sealed while reducing the pressure to 0.1 atm, and a lithium ion secondary battery was obtained.
In the lithium ion secondary battery fabricated in the same manner, the active material layer of the electrode element after the heat-drying step was quickly taken out and cut finely, and the content of physically adsorbed water was calculated by the Karl Fischer method at 150° C.
The prepared secondary battery was charged at 1° C. up to 4.2 V and then at constant voltage for 2.5 hours in total in a thermostat kept at 25° C., and discharged at 1° C. to 2.5 V as constant current discharge. This cycle was repeated 300 times at 45° C. The ratio of the discharge capacity after 300 cycles to the initial discharge capacity was determined as the capacity retention ratio.
The results are shown in Table 1.
The electrode element produced in the same manner as in Example 1was not accommodated in an aluminum laminate outer package, and heat-dried for 6 hours in an environment under a dry nitrogen atmosphere while maintaining the temperature condition at 90° C. Next, the dried electrode element was quickly placed, in an aluminum laminate outer package, and the electrolyte solution was injected. The outer package was sealed while reducing the pressure to 0.1 atm to manufacture a lithium ion secondary battery, which was evaluated. All steps after drying of the electrode element are carried out under humidity of 0.6 RH % or less.
A lithium ion secondary battery was prepared and evaluated in the same manner as in Example 1 except that a metal, can was used in place of the aluminum laminate outer package and heat drying was performed at 150° C.
A lithium ion secondary battery was obtained and evaluated in the same manner as in Example 1 except that heat drying at 90 to 100° C. was not carried out.
A lithium ion secondary battery was prepared and evaluated in the same manner as in Example 1 except that a polypropylene microporous membrane (heat shrinking ratio of 2% by heat treatment at 90° C. for 60 hours) was used as a separator in place of the aramid microporous membrane. Since the initial charge/discharge capacity of the battery of Reference Example 2 was 100 mAh or less, no subsequent evaluation was made.
The lithium ion secondary batteries of Example 3 and Reference Example 1, each after 300 cycles, were disassembled under an environment having a dew point of minus 40° C. or lower, and the positive electrode active material layers were recovered, the positive electrode active materials were preliminarily dried by keeping under nitrogen atmosphere at 150° C. for 1 hour, and weighed and then kept at 260° C. for 30 minutes to allow to generation water. The chemically adsorbed water ratio was determined by the Karl Fischer coulometric titration method by measuring the amount of the generated water.
The results are shown in Table 1.
The battery according to the present invention can be utilized in, for example, ail the industrial fields requiring a power supply and the industrial fields pertaining to the transportation, storage and supply of electric energy. Specifically, it can be used in, for example, power supplies for mobile equipment such as cellular phones and notebook personal computers; power supplies for moving/transporting media such as trains, satellites and submarines including electrically driven, vehicles such as an electric vehicle, a hybrid vehicle, an electric motorbike, and an electric-assisted bike; backup power supplies for UPSs; and electricity storage facilities for storing electric power generated by photovoltaic power generation, wind power generation and the like.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2015-061781 | Mar 2015 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2016/059049 | 3/22/2016 | WO | 00 |
