WO2011096564A1 - 二次電池用ゲル電解質複合フィルム、及び、二次電池 - Google Patents
二次電池用ゲル電解質複合フィルム、及び、二次電池 Download PDFInfo
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- WO2011096564A1 WO2011096564A1 PCT/JP2011/052533 JP2011052533W WO2011096564A1 WO 2011096564 A1 WO2011096564 A1 WO 2011096564A1 JP 2011052533 W JP2011052533 W JP 2011052533W WO 2011096564 A1 WO2011096564 A1 WO 2011096564A1
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- secondary battery
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- gel electrolyte
- vinylidene fluoride
- vdf
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0564—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
- H01M10/0565—Polymeric materials, e.g. gel-type or solid-type
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
- H01B1/00—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
- H01B1/06—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors mainly consisting of other non-metallic substances
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
- H01B1/00—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
- H01B1/06—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors mainly consisting of other non-metallic substances
- H01B1/12—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors mainly consisting of other non-metallic substances organic substances
- H01B1/122—Ionic conductors
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0085—Immobilising or gelification of electrolyte
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0088—Composites
- H01M2300/0091—Composites in the form of mixtures
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Definitions
- the present invention relates to a gel electrolyte composite film for a secondary battery that has improved ion conductivity, excellent ignition resistance, and is difficult to be colored, and a secondary battery using the same.
- Secondary batteries particularly lithium secondary batteries, such as electric vehicles (EV), are strongly required to improve their performance as one of the decisive factors for global warming countermeasures.
- EV electric vehicles
- a lithium secondary battery has a basic structure in which a non-aqueous electrolyte is disposed between a positive electrode and a negative electrode via a separator, if necessary, and a solid state and a type using an electrolyte dissolved in a solvent. It is roughly divided into types that use electrolytes. Further, the type using an electrolytic solution includes a type in which the electrolytic solution is sealed as it is and a gel electrolyte type in which the electrolytic solution is held in a polymer gel film.
- Electrolyte holding film that constitutes the gel electrolyte is required to safely and not degrade the electrical properties of the electrolyte. From these viewpoints, the electrolyte holding ability is high, ion conductivity is high, It is required to be mechanically and chemically stable and to have excellent mechanical strength.
- Patent Documents 1 to 11 In response to these requirements, non-fluorinated polyether resins have been used in the past, but it is difficult to respond to higher performance in terms of safety and ionic conductivity, making them thermally and chemically stable. New fluoropolymers have been investigated (Patent Documents 1 to 11).
- Patent Documents 1 and 2 describe an electrolyte solution holding film using a copolymer of vinylidene fluoride (VdF) and hexafluoropropylene (HFP).
- VdF vinylidene fluoride
- HFP hexafluoropropylene
- the VdF / HFP copolymers described in these patent documents have a high electrolyte solution retention property, but the swelling to the electrolyte solution is particularly severe at high temperatures, which causes battery cell swelling.
- Patent Document 3 it is proposed to use a fluorine-based segmented polymer composed of a segment that imparts membrane strength and a segment that wets the electrolyte in order to achieve both electrolyte retention and membrane strength.
- Patent Document 4 the use of a VdF copolymer elastomer of 35 to 85 mol% VdF, 13 to 45 mol% HFP, and 0 to 35 mol% tetrafluoroethylene (TFE) allows the retention of electrolyte and the strength of the film. To achieve both.
- Patent Documents 5 and 6 a proposal using a polymer composition (polymer alloy) in which a VdF copolymer, polyvinylidene fluoride (PVdF) and polyoxyethylene (PEO), etc. are mixed (Patent Documents 5 and 6), a PVdF-PMVE copolymer is used. Proposal for improving film strength (Patent Document 7), Proposal using PVdF having PEO or acrylate in the side chain (Patent Document 8), Proposal for making porous film by crosslinking PVdF or VdF / HFP copolymer (Patent Documents 9 and 10).
- Patent Document 11 relating to a binder for a secondary battery and a battery mixture suggests that a copolymer of VdF and TFE is useful as a polymer gel electrolyte.
- Patent Document 12 relating to a polymer electrolyte secondary battery includes a PVdF copolymer containing PVdF as a main component as a polymer resin for a gel polymer electrolyte.
- Patent Document 13 discloses a repeating unit of 35 to 99 mol% derived from VdF, which is derived from TFE, for the purpose of providing a polymer electrolyte excellent in film strength, heat resistance and nonaqueous electrolyte retention.
- Patent Document 13 does not describe a composite film composed of a polymer electrolyte and a porous film.
- Patent Document 14 discloses a porous reinforcing member (A) made of a high-strength heat-resistant resin and having a thickness of 100 ⁇ m or less, a repeating unit derived from VdF held in the porous reinforcing member, 50 to 99 mol%, from TFE.
- VdF copolymer (B) consisting of 1 to 50 mol% of derived repeating units, having a melting point of 80 ° C.
- an electrolytic solution (C) composed of a shaped polar organic solvent (c1) and an electrolyte (c2), having a thickness of 200 ⁇ m or less, an ionic conductivity of 0.05 S / m (25 ° C.) or more, and a puncture strength of 100 g
- an electrolyte-supported polymer film having a mechanical heat resistant temperature of 200 ° C. or higher is described.
- Patent Document 14 for the purpose of providing an electrolyte-supported polymer film for a lithium ion secondary battery with high safety at the time of overcharging, which combines ionic conductivity, strength, and heat resistance.
- Aromatic polyamide is used as the high strength heat resistant resin.
- the conventional separator is usually made of polyethylene, polypropylene or the like, and has ignitability.
- the battery is operated at a high voltage or high temperature, a phenomenon occurs in which the positive electrode side is denatured and colored.
- An object of the present invention is to provide a gel electrolyte composite film for a secondary battery that has improved ion conductivity, is excellent in ignition resistance, and is difficult to be colored.
- the present invention includes vinylidene fluoride units and tetrafluoroethylene units in a molar ratio of 55/45 to 95/5 of vinylidene fluoride units / tetrafluoroethylene units, and 0 to 10 mol% of hexafluoropropylene units. (However, the total amount of vinylidene fluoride units, tetrafluoroethylene units, and hexafluoropropylene units is 100 mol%) A nonaqueous electrolyte solution is impregnated in an electrolyte solution holding film containing a vinylidene fluoride copolymer resin.
- the gel electrolyte composite film for secondary batteries which consists of the gel electrolyte for secondary batteries which consists of, and the porous film which consists of at least 1 sort (s) of resin chosen from the group which consists of polyethylene, a polypropylene, and a polyimide.
- the vinylidene fluoride copolymer resin is preferably a vinylidene fluoride binary copolymer resin composed only of vinylidene fluoride units and tetrafluoroethylene units.
- the vinylidene fluoride copolymer resin is preferably a vinylidene fluoride terpolymer resin containing 1 to 5 mol% of hexafluoropropylene units.
- the electrolytic solution holding film preferably contains a resin other than the vinylidene fluoride-based copolymer resin and / or rubber.
- the other resin is preferably polyacrylonitrile, polyamideimide, polyvinylidene fluoride, tetrafluoroethylene / hexafluoropropylene copolymer resin, or a mixed resin of two or more of these.
- the other rubber is preferably vinylidene fluoride / hexafluoropropylene copolymer rubber, vinylidene fluoride / tetrafluoroethylene / hexafluoropropylene copolymer rubber, acrylic rubber, or a mixture of two or more of these. .
- the content of the other resin and / or rubber is preferably 400 parts by mass or less with respect to 100 parts by mass of the vinylidene fluoride copolymer resin.
- the electrolytic solution holding film preferably contains metal oxide particles.
- the metal oxide particles are preferably aluminum oxide particles or silicon oxide particles.
- the average particle diameter of the metal oxide particles is preferably 20 ⁇ m or less.
- the present invention also relates to a secondary battery comprising a gel electrolyte composite film for a secondary battery and an electrode.
- the ion conductivity improves, Furthermore, it is excellent in ignition resistance, and the gel electrolyte composite film for secondary batteries which is hard to be colored, and the secondary battery using this gel electrolyte composite film for secondary batteries In particular, a lithium secondary battery can be provided.
- the gel electrolyte composite film for a secondary battery of the present invention comprises a gel electrolyte for a secondary battery and a porous film.
- the gel electrolyte for a secondary battery is obtained by impregnating a non-aqueous electrolyte into an electrolyte holding film containing a specific VdF / TFE copolymer resin.
- the electrolytic solution holding film used in the present invention contains VdF units and TFE units in a molar ratio of VdF units / TFE units of 55/45 to 95/5 and HFP units of 0 to 10 mol% (however, VdF units And the total amount of TFE units and HFP units is 100 mol%).
- VdF / TFE copolymer resin is a molar ratio of VdF units / TFE units of 55/45 to 95/5 and HFP units of 0 to 10 mol% (however, VdF units And the total amount of TFE units and HFP units is 100 mol%).
- VdF / TFE copolymer resin examples include a VdF / TFE binary copolymer and a VdF / TFE / HFP ternary copolymer.
- the molar ratio of VdF units / TFE units is 55/45 to 95/5.
- the molar ratio of VdF unit / TFE unit is less than 55/45, it is not preferable because the swelling property to the electrolytic solution is low and the solubility to the solvent is also low, so that it is difficult to form a film.
- the lower limit of the VdF unit / TFE unit is 55/45 in terms of molar ratio, and 60/40 is preferable because the elongation is good and the swelling property to the electrolytic solution is appropriately low.
- the upper limit is 95/5, but if it is larger than this, the elongation becomes smaller, and since it can only be dissolved in amide-type high-boiling solvents such as N-methylpyrrolidone and dimethylformamide, the degree of freedom in forming the film becomes narrower. It is not preferable.
- the upper limit of VdF units / TFE units is 95/5 in molar ratio, more preferably 90/10, and particularly preferably 85/15.
- the VdF unit / TFE unit is 55/45 to 95/5 in a molar ratio, and the HFP unit is contained in an amount of 10 mol% or less.
- the molar ratio of VdF unit / TFE unit is less than 55/45, it is not preferable because the swelling property to the electrolytic solution is low and the solubility to the solvent is also low, so that it is difficult to form a film.
- the lower limit of the VdF unit / TFE unit is preferably 60/40 in terms of molar ratio because the elongation is good and the swelling property to the electrolytic solution is appropriately low.
- the upper limit is 95/5, but if it is larger than this, the elongation becomes smaller, and since it can only be dissolved in amide-type high-boiling solvents such as N-methylpyrrolidone and dimethylformamide, the degree of freedom in forming the film becomes narrower. It is not preferable. If the HFP unit exceeds 10 mol%, the swelling property to the electrolyte is increased, which is not preferable.
- the preferred HFP unit content is 5 mol% or less, and further 4 mol% or less. The minimum with preferable content of a HFP unit is 1 mol%.
- the ionic conductivity is not determined only by the swellability, but also depends on the crystallinity of the polymer.
- the PVFE has a low swell ratio but the crystallinity of the TFE / VdF / HFP copolymer. Some have high ionic conductivity because of low.
- the VdF / TFE copolymer resin preferably has a melting point of 100 to 200 ° C.
- fusing point can be calculated
- DSC differential scanning calorimetry
- the resin has a melting point at room temperature (for example, 25 ° C.) or higher, and the rubber does not have a clear melting point at room temperature or higher.
- preferable resins used in combination include polyacrylonitrile, polyamideimide, polyvinylidene fluoride (PVdF), one or more of VdF / HFP copolymer resins, and preferable rubbers include, for example, VdF / HFP.
- VdF / HFP One type or two or more types of copolymer rubber, VdF / TFE / HFP copolymer rubber, acrylic rubber and the like can be used. These rubbers may or may not be cross-linked.
- acrylic rubber is particularly preferable from the viewpoint of improving ion conductivity
- VdF / HFP copolymer rubber is preferable from the viewpoint of improving ion conductivity and oxidation resistance.
- examples thereof include VdF / TFE / HFP copolymer rubber and VdF / HFP resin.
- the VdF / HFP copolymer rubber preferably has a VdF unit / HFP unit in a molar ratio of 80/20 to 65/35.
- the VdF / TFE / HFP copolymer rubber preferably has a molar ratio of VdF units / TFE units / HFP units of 80/5/15 to 60/30/10.
- the VdF / HFP resin preferably has a molar ratio of VdF units / HFP units of 98/2 to 85/15.
- the VdF / HFP resin preferably has a melting point of 100 to 200 ° C.
- the compounding amount of the other resin or rubber is preferably 400 parts by mass or less, more preferably 200 parts by mass or less, still more preferably 150 parts by mass or less with respect to 100 parts by mass of the specific VdF / TFE copolymer resin. is there.
- the lower limit varies depending on the intended effect, but is about 10 parts by mass.
- the electrolytic solution holding film may contain metal oxide particles.
- the metal oxide is not particularly limited, but an oxide other than alkali metal or alkaline earth metal is preferable from the viewpoint of improving ion conductivity and shutdown effect, and particularly aluminum oxide, silicon oxide, titanium oxide, vanadium oxide, copper oxide, and the like. Is preferred.
- the particle diameter fine particles having an average particle diameter of 20 ⁇ m or less, further 10 ⁇ m or less, and particularly 5 ⁇ m or less are preferable.
- Particularly preferable metal oxide particles are aluminum oxide particles or silicon oxide particles having an average particle diameter of 5 ⁇ m or less from the viewpoint of excellent ion conductivity.
- the production of the electrolytic solution holding film is not particularly limited, and a conventionally known method can be adopted. Specifically, a method in which a VdF / TFE copolymer is dissolved in a solvent, cast on a film having a smooth surface such as a polyester film or an aluminum film, and then peeled off can be exemplified. Moreover, you may apply
- amide solvents such as N-methyl-2-pyrrolidone, dimethylformamide and dimethylacetamide
- ketone solvents such as methyl isobutyl ketone, methyl ethyl ketone and cyclohexanone
- cyclic ether solvents such as tetrahydrofuran and methyltetrahydrofuran can be used.
- PVdF is soluble only in high-boiling and high-polar amide solvents, but VdF / TFE copolymers are soluble in lower-boiling and low-polar ketones and cyclic ethers. It is desirable to use a low polarity solvent.
- the thickness of the electrolytic solution holding film may be a normal thickness of about 5 to 50 ⁇ m.
- This electrolyte solution holding film can also be used alone.
- the gel electrolyte composite film for a secondary battery of the present invention is a composite of the electrolytic solution holding film and the porous film.
- the porous film is a resin film made of at least one resin selected from the group consisting of polyethylene, polypropylene, and polyimide.
- the porous film preferably has a total weight of polyethylene, polypropylene and polyimide of 50% by mass or more of the porous film. More preferably, the porous film is made of polyethylene.
- the porous film may further be made of polyamide, polyamideimide or the like.
- porous film a porous film obtained by casting polyethylene, polypropylene, polyimide, and, if necessary, polyamide, polyamideimide, etc. to a nonwoven fabric; or a mixture of these synthetic resins and water-soluble inorganic oxides After that, a film obtained by forming a film and then making it porous by a method such as removing inorganic oxides by washing with water is preferable because the electrolyte can easily permeate and has high ionic conductivity.
- a method of roll coating a VdF / TFE copolymer solution on a porous film a method of dipping into a VdF / TFE copolymer solution, and the like are preferable.
- the gel electrolyte composite film for a secondary battery As the gel electrolyte composite film for a secondary battery, a form in which the gel electrolyte polymer solution of the present application is applied or dipped on a conventional separator and the separator is covered with an electrolyte holding film layer is preferable.
- Conventional separators made of polyethylene, polypropylene or polyimide are ignitable.
- the battery is operated at a high voltage or high temperature, a phenomenon occurs in which the positive electrode side is denatured and colored, but the ignitability can be suppressed by forming an electrolyte solution holding film layer on the separator.
- the coloring of the separator at a high voltage or high temperature can be suppressed by applying to the positive electrode side.
- a solution obtained by dissolving a known electrolyte salt in a known electrolyte salt dissolving organic solvent can be used.
- the organic solvent for dissolving the electrolyte is not particularly limited, but propylene carbonate, ethylene carbonate, butylene carbonate, ⁇ -butyrolactone, 1,2-dimethoxyethane, 1,2-diethoxyethane, dimethyl carbonate, diethyl carbonate
- Known hydrocarbon solvents such as fluorinated solvents such as fluoroethylene carbonate, fluoroether, and fluorinated carbonate can be used.
- Examples of the electrolyte salt include LiClO 4 , LiAsF 6 , LiBF 4 , LiPF 6 , LiN (SO 2 CF 3 ) 2 , LiN (SO 2 C 2 F 5 ) 2 and the like for lithium secondary batteries. From the viewpoint of good cycle characteristics, LiPF 6 , LiBF 4 , LiN (SO 2 CF 3 ) 2 , LiN (SO 2 C 2 F 5 ) 2 or a combination thereof is particularly preferable.
- the concentration of the electrolyte salt is required to be 0.8 mol / liter or more, and further 1.0 mol / liter or more. Although the upper limit depends on the organic solvent for dissolving the electrolyte salt, it is usually 1.5 mol / liter.
- the secondary battery of the present invention can be produced by enclosing and sealing the positive and negative electrodes and the gel electrolyte of the present invention in a battery case.
- known active materials for lithium secondary batteries may be used as the positive electrode and the negative electrode.
- a separator may be interposed between the positive electrode and the negative electrode.
- Reference example 1 A TFE / VdF / HFP (38/60/2 mol% ratio) copolymer was dissolved in tetrahydrofuran (THF), applied to a polyester (PET) film, dried at 100 ° C. for 15 minutes, and then peeled off. An electrolytic solution holding film (electrolytic solution holding film 1) having a thickness of 30 ⁇ m was produced. The melting point of the polymer was 140 ° C.
- Dumbbells (5 cm ⁇ 3 cm strips) were prepared from the obtained electrolyte solution-holding film 1 and the tensile elongation at break was measured with a tensile tester (RTC-1225A manufactured by Orientec Corp.). The results are shown in Table 1.
- Electrolytic solution swelling Cut the electrolytic solution holding film to a size of 5 ⁇ 20 mm, and put it in a sample bottle containing the electrolytic solution (a solution of LiPF 6 dissolved at a concentration of 1M in 3/7 (volume ratio) solvent of ethylene carbonate and ethyl methyl carbonate). The mixture is allowed to stand at 90 ° C. for 2 days, and the mass increase (%) from before introduction is calculated.
- the electrolytic solution holding film is immersed in an electrolytic solution (a solution of LiPF 6 dissolved in 3/7 (volume ratio) of ethylene carbonate and ethyl methyl carbonate at a concentration of 1 M) for 10 minutes, and then sandwiched between SUS electrodes, and galvano potency.
- Ionic conductivity (S) by AC impedance method (frequency: 10 ⁇ 3 to 10 6 Hz, AC voltage: 10 mV) connected to Ostat (frequency analyzer: Model 1260 manufactured by Solartron, potentiostat: Model 1287 manufactured by Solartron) / Cm).
- a slurry dispersed in pyrrolidone was uniformly applied on a positive electrode current collector (aluminum foil having a thickness of 20 ⁇ m) and dried to prepare a positive electrode.
- This positive electrode was used in the following high temperature test.
- a positive electrode in the next high-voltage test a positive electrode produced by the same procedure as described above was used except that the positive electrode active material was changed to LiNi 0.5 Mn 1.5 O 4 .
- the produced positive electrode and negative electrode were each cut into a rectangle of 50 mm ⁇ 100 mm, and the electrolyte solution holding film 1 produced above was sandwiched between the positive electrode / negative electrode as a separator to obtain a laminate.
- this laminate was made of the above electrolyte solution (3/7 (volume ratio) of ethylene carbonate (EC) and ethyl methyl carbonate (EMC)).
- EC ethylene carbonate
- EMC ethyl methyl carbonate
- Comparative Example 1 In Reference Example 1, as the electrolytic solution holding film, except that the comparative electrolytic solution holding film 1 produced by the following method was used, the tensile elongation at break, the electrolytic solution swelling rate, the ionic conductivity, the ignitability, and the high temperature operation The coloring at the time and the coloring at the time of high voltage operation were examined. The results are shown in Table 1.
- PVdF was dissolved in N-methyl-2-pyrrolidone (NMP), applied to a PET film, dried at 100 ° C. for 30 minutes, and then peeled to prepare a comparative electrolyte holding film 1 having a thickness of 30 ⁇ m.
- NMP N-methyl-2-pyrrolidone
- Comparative Example 2 In Reference Example 1, as the electrolytic solution holding film, except that the comparative electrolytic solution holding film 2 produced by the following method was used, the tensile elongation at break, the electrolytic solution swelling rate, the ionic conductivity, the ignitability, and the high temperature operation The coloring at the time and the coloring at the time of high voltage operation were examined. The results are shown in Table 1.
- Comparative Electrolyte Holding Film 2 (Preparation of Comparative Electrolyte Holding Film 2) A VdF / HFP (88/12 mol% ratio) copolymer was dissolved in NMP, applied to a PET film, dried at 100 ° C. for 30 minutes, and then peeled off. A comparative electrolyte holding film 2 having a thickness of 30 ⁇ m was made.
- the TFE / VdF copolymer and the TFE / VdF / HFP copolymer have higher elongation than the PVdF and VdF / HFP copolymer, and high ion conductivity even when the swelling rate is low.
- Reference Examples 3-10 In Reference Example 1, the electrolytic solution holding films 3 to 10 produced by the following method were used as the electrolytic solution holding film in the same manner, and the tensile breaking elongation, the electrolytic solution swelling rate, the ionic conductivity, the ignitability, the high temperature The coloring during operation and the coloring during high voltage operation were investigated. The results are shown in Table 2.
- the TFE / VdF copolymer resin can maintain high ionic conductivity by adjusting the swelling rate while maintaining elongation by blending different compositions, and there is no ignitability. It can be seen that there is no coloration at high temperature / high voltage operation. Furthermore, it turns out that ionic conductivity can be improved by combining with acrylic fine particles / acrylonitrile, silica / alumina and the like.
- Comparative Example 3 In the same manner as in Example 1, except that a polyethylene separator (thickness 22 ⁇ m) not covered with the electrolyte holding film layer was used, ion conductivity, ignitability, coloring at high temperature operation, and high voltage operation The coloring of the time was examined. The results are shown in Table 3.
- Example 7 TFE / VdF / HFP (38/60/2 mol% ratio) copolymer and TFE / VdF / HFP (6/77/17 mol% ratio) copolymer rubber were blended at a mass ratio of 50/50. The blend was dissolved in THF, applied to the positive electrode prepared in Reference Example 1, and dried at 80 ° C. for 15 minutes to prepare a positive electrode covered with an electrolyte solution holding film layer having a thickness of about 2 ⁇ m. A laminate cell was prepared in the same manner as in Reference Example 1 except that a polyethylene separator (thickness: 22 ⁇ m) was used as the separator using this electrolytic solution holding film-covered positive electrode. No coloring was observed.
- Example 8 LiPF 6 was dissolved at a concentration of 1M in EC / dimethyl carbonate (DMC) / EMC / HCF 2 CF 2 CH 2 OCF 2 CF 2 H (volume ratio 20/50/10/20) as an electrolytic solution. Except for using electrolyte solution containing 0.1% by mass of vinylene carbonate (VC) and 3% by mass of fluoroethylene carbonate (FEC) as an additive to the electrolyte solution, and using electrolytic solution holding film-coated separator 3 as a separator. A laminate cell was prepared in the same manner as in Reference Example 1, and a high temperature test was conducted under the following conditions to examine the presence or absence of coloring of the separator and the capacity retention rate. The results are shown in Table 4.
- Example 8 as an electrolytic solution, added to an electrolytic solution obtained by dissolving LiPF 6 at a concentration of 1M in EC / DMC / EMC / HCF 2 CF 2 CH 2 OCF 2 CF 2 H (volume ratio 20/50/10/20).
- VC vinylene carbonate
- FEC fluoroethylene carbonate
- Example 8 conducted a high temperature test in Example 8 to examine the presence or absence of coloring of the separator and the capacity retention rate. The results are shown in Table 4.
- Example 9 an electrolytic solution holding film-coated separator 3 was used as a separator in the same manner as in Example 8, except that an electrolytic solution in which LiPF 6 was dissolved at a concentration of 1 M in EC / EMC (volume ratio 30/70) was used.
- a laminate cell was prepared using the above, a high temperature test of Example 8 was performed, and the presence or absence of coloring of the separator and the capacity retention rate were examined. The results are shown in Table 4.
- Example 9 a laminate cell was prepared in the same manner as in Example 9 except that a polyethylene separator before being coated with the electrolytic solution holding film was used as the separator, and the high temperature test of Example 8 was performed. Existence and capacity maintenance rate were examined. The results are shown in Table 4.
- Example 10 In Example 8, a laminate cell was prepared in the same manner as in Example 8 except that the electrolytic solution holding film-coated separator 6 was used as the electrolytic solution holding film-coated separator, and the high-temperature test in Example 8 was performed. Existence and capacity maintenance rate were examined. The results are shown in Table 4.
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Abstract
Description
VdF/TFE/HFP共重合体ゴムは、VdF単位/TFE単位/HFP単位がモル比で80/5/15~60/30/10であることが好ましい。
VdF/HFP樹脂は、VdF単位/HFP単位がモル比で98/2~85/15であることが好ましい。
VdF/HFP樹脂は、融点が100~200℃であることが好ましい。
TFE/VdF/HFP(38/60/2モル%比)共重合体をテトラヒドロフラン(THF)に溶解させ、ポリエステル(PET)フィルムに塗布し、100℃にて15分間乾燥させたのちに剥離し、厚さ30μmの電解液保持フィルム(電解液保持フィルム1)を作製した。当該ポリマーの融点は140℃であった。
電解液保持フィルムを5×20mmの大きさに切り取り、電解液(エチレンカーボネートとエチルメチルカーボネートの3/7(体積比)の溶媒にLiPF6を1M濃度で溶解した溶液)が入ったサンプル瓶に入れ、90℃で2日間静置し、投入前からの質量増加(%)を算出する。
電解液保持フィルムを電解液(エチレンカーボネートとエチルメチルカーボネートの3/7(体積比)の溶媒にLiPF6を1M濃度で溶解した溶液)に10分間浸漬したのち、SUS電極で挟み、ガルバノ・ポテンシオスタット(周波数アナライザー:ソーラトロン社製1260型、ポテンシオスタット:ソーラトロン社製1287型)に接続し交流インピーダンス法(周波数:10-3~106Hz、交流電圧:10mV)よりイオン伝導度(S/cm)を測定する。
電解液保持フィルムを電解液(エチレンカーボネートとエチルメチルカーボネートの3/7(体積比)の溶媒にLiPF6を1M濃度で溶解した溶液)に10分間浸漬したのち、アルコールランプの炎であぶり、着火するかどうかを観察する。
<正極の作製>
Li2Mn2O4とカーボンブラックとポリフッ化ビニリデン((株)クレハ製。商品名KF-1000)を94/3/3(質量%比)で混合した正極活物質をN-メチル-2-ピロリドンに分散してスラリー状としたものを正極集電体(厚さ20μmのアルミニウム箔)上に均一に塗布し、乾燥して正極を作製した。この正極はつぎの高温試験の場合に用いた。一方、つぎの高電圧試験の際の正極としては、正極活物質をLiNi0.5Mn1.5O4に変えたほかは上記と同様の手順にて作製した正極を用いた。
人造黒鉛粉末(日立化成(株)製。商品名MAG-D)に、蒸留水で分散させたスチレン-ブタジエンゴムを固形分で6質量%となるように加え、ディスパーザーで混合してスラリー状としたものを負極集電体(厚さ18μmのアルミニウム箔)上に均一に塗布し、乾燥して負極を作製した。
つぎの充放電測定条件で60℃に保持し、50サイクル後の電解液保持フィルムの着色の有無を観察する。
充放電電圧:2.5~4.2V
充電:0.5C、4.2Vにて充電電流が1/10になるまで一定電圧を保持
放電:0.5C
つぎの充放電測定条件で50サイクル後の電解液保持フィルムの着色の有無を観察する。
充放電電圧:2.5~4.9V
充電:0.5C、4.9Vにて充電電流が1/10になるまで一定電圧を保持
放電:0.5C
参考例1において、電解液保持フィルムとして、つぎの方法で作製した電解液保持フィルム2を用いたほかは同様にして、引張破断伸び、電解液膨潤率、イオン伝導度、着火性、高温動作時の着色、および高電圧動作時の着色を調べた。結果を表1に示す。
TFE/VdF(20/80モル%比)共重合体をメチルイソブチルケトンに溶解させ、PETフィルムに塗布し、100℃にて15分間乾燥させたのちに剥離し、厚さ30μmの電解液保持フィルム2を作製した。当該ポリマーの融点は120℃であった。
参考例1において、電解液保持フィルムとして、つぎの方法で作製した比較電解液保持フィルム1を用いたほかは同様にして、引張破断伸び、電解液膨潤率、イオン伝導度、着火性、高温動作時の着色、および高電圧動作時の着色を調べた。結果を表1に示す。
PVdFをN-メチル-2-ピロリドン(NMP)に溶解させ、PETフィルムに塗布し、100℃にて30分間乾燥させたのちに剥離し、厚さ30μmの比較電解液保持フィルム1を作製した。
参考例1において、電解液保持フィルムとして、つぎの方法で作製した比較電解液保持フィルム2を用いたほかは同様にして、引張破断伸び、電解液膨潤率、イオン伝導度、着火性、高温動作時の着色、および高電圧動作時の着色を調べた。結果を表1に示す。
VdF/HFP(88/12モル%比)共重合体をNMPに溶解させ、PETフィルムに塗布し、100℃にて30分間乾燥させたのちに剥離し、厚さ30μmの比較電解液保持フィルム2を作製した。
参考例1において、電解液保持フィルムとして、つぎの方法で作製した電解液保持フィルム3~10を用いたほかは同様にして、引張破断伸び、電解液膨潤率、イオン伝導度、着火性、高温動作時の着色、および高電圧動作時の着色を調べた。結果を表2に示す。
TFE/VdF/HFP(38/60/2モル%比)共重合体とTFE/VdF/HFP(6/77/17モル%比)共重合体ゴムを質量比で75/25でブレンドし、このブレンド物をTHFに溶解させ、PETフィルムに塗布し、100℃にて15分間乾燥させたのちに剥離し、厚さ30μmの電解液保持フィルム3を作製した。共重合体ゴムでは室温以上で明確な融点は観測できなかった。
TFE/VdF/HFP(38/60/2モル%比)共重合体とTFE/VdF/HFP(6/77/17モル%比)共重合体ゴムを質量比で50/50でブレンドし、このブレンド物をTHFに溶解させ、PETフィルムに塗布し、100℃にて15分間乾燥させたのちに剥離し、厚さ30μmの電解液保持フィルム4を作製した。共重合体ゴムでは室温以上で明確な融点は観測できなかった。
TFE/VdF/HFP(38/60/2モル%比)共重合体とVdF/HFP(78/22モル%比)共重合体を質量比で75/25でブレンドし、このブレンド物をTHFに溶解させ、PETフィルムに塗布し、100℃にて15分間乾燥させたのちに剥離し、厚さ30μmの電解液保持フィルム5を作製した。このVdF/HFP(78/22)共重合体ゴムでは室温以上で明確な融点は観測できなかった。
TFE/VdF/HFP(38/60/2モル%比)共重合体とVdF/HFP(78/22モル%比)共重合体を質量比で50/50でブレンドし、このブレンド物をTHFに溶解させ、PETフィルムに塗布し、100℃にて15分間乾燥させたのちに剥離し、厚さ30μmの電解液保持フィルム6を作製した。このVdF/HFP(78/22)共重合体ゴムでは室温以上で明確な融点は観測できなかった。
TFE/VdF/HFP(38/60/2モル%比)共重合体とアクリルゴム粒子(三菱レイヨン(株)製のW450A)を質量比で80/20でブレンドし、このブレンド物をTHFに溶解させ、PETフィルムに塗布し、100℃にて15分間乾燥させたのちに剥離し、厚さ30μmの電解液保持フィルム7を作製した。
TFE/VdF/HFP(38/60/2モル%比)共重合体とポリアクリロニトリル粒子(アルドリッチ社製のポリアクリロニトリル)を質量比で80/20でブレンドし、このブレンド物をTHFに溶解させ、PETフィルムに塗布し、100℃にて15分間乾燥させたのちに剥離し、厚さ30μmの電解液保持フィルム8を作製した。
TFE/VdF/HFP(38/60/2モル%比)共重合体とSiO2粒子(扶桑化学工業(株)製のSP03F。粒子径約0.3μm)を質量比で90/10でブレンドし、このブレンド物をTHFに溶解させ、PETフィルムに塗布し、100℃にて15分間乾燥させたのちに剥離し、厚さ30μmの電解液保持フィルム9を作製した。
TFE/VdF/HFP(38/60/2モル%比)共重合体とAl2O3粒子(マイクロン(株)製のAX3-15。粒子径約0.3μm)を質量比で90/10でブレンドし、このブレンド物をTHFに溶解させ、PETフィルムに塗布し、100℃にて15分間乾燥させたのちに剥離し、厚さ30μmの電解液保持フィルム10を作製した。
参考例1において、電解液保持フィルムに代えて、つぎの方法で作製した電解液保持フィルム被覆セパレータ1~6を用いたほかは同様にして、イオン伝導度、着火性、高温動作時の着色、および高電圧動作時の着色を調べた。結果を表3に示す。
TFE/VdF/HFP(38/60/2モル%比)共重合体をTHFに溶解させ、ポリエチレン製のセパレータ(厚さ22μm)に塗布し、80℃にて15分間乾燥させて、電解液保持フィルム層(厚さ1μm)で被覆されたセパレータ1を作製した(セパレータ/電解液保持フィルム層中のVdF/TFE系共重合体の質量比:約1/0.5)。
TFE/VdF/HFP(38/60/2モル%比)共重合体とTFE/VdF/HFP(6/77/17モル%比)共重合体ゴムを質量比で75/25でブレンドし、このブレンド物をTHFに溶解させ、ポリエチレン製のセパレータ(厚さ22μm)に塗布し、80℃にて15分間乾燥させて、電解液保持フィルム層で被覆された厚さ23μmのセパレータ2を作製した(セパレータ/電解液保持フィルム層中のVdF/TFE系共重合体の質量比:約1/0.5)。
TFE/VdF/HFP(38/60/2モル%比)共重合体とTFE/VdF/HFP(6/77/17モル%比)共重合体ゴムを質量比で50/50でブレンドし、このブレンド物をTHFに溶解させ、ポリエチレン製のセパレータ(厚さ22μm)に塗布し、80℃にて15分間乾燥させて、電解液保持フィルム層(厚さ1μm)で被覆されたセパレータ3を作製した(セパレータ/電解液保持フィルム層中のVdF/TFE系共重合体の質量比:約1/0.5)。
TFE/VdF/HFP(38/60/2モル%比)共重合体とアクリルゴム粒子(三菱レイヨン(株)製のW-450A)を質量比で80/20でブレンドし、このブレンド物をTHFに溶解させ、ポリエチレン製のセパレータ(厚さ22μm)に塗布し、80℃にて15分間乾燥させて、電解液保持フィルム層(厚さ1μm)で被覆されたセパレータ4を作製した(セパレータ/電解液保持フィルム層中のVdF/TFE系共重合体の質量比:約1/0.5)。
TFE/VdF/HFP(38/60/2モル%比)共重合体とTFE/VdF/HFP(6/77/17モル%比)共重合体ゴムを質量比で50/50でブレンドし、さらにAl2O3粒子(マイクロン(株)製のAX3-15。粒子径約0.3μm)をブレンド物に対して10質量%となるようにブレンドし、得られたブレンド物をTHFに溶解させ、ポリエチレン製のセパレータ(厚さ22μm)に塗布し、80℃にて15分間乾燥させて、電解液保持フィルム層(厚さ1μm)で被覆されたセパレータ5を作製した(セパレータ/電解液保持フィルム層中のVdF/TFE系共重合体の質量比:約1/0.5)。
TFE/VdF/HFP(38/60/2モル%比)共重合体とTFE/VdF/HFP(6/77/17モル%比)共重合体ゴムを質量比で25/75でブレンドし、このブレンド物をTHFに溶解させ、ポリエチレン製のセパレータ(厚さ22μm)に塗布し、80℃にて15分間乾燥させて、電解液保持フィルム層(厚さ1μm)で被覆されたセパレータ3を作製した(セパレータ/電解液保持フィルム層中のVdF/TFE系共重合体の質量比:約1/0.5)。
実施例1において、電解液保持フィルム層で被覆されていないポリエチレン製のセパレータ(厚さ22μm)を用いたほかは同様にして、イオン伝導度、着火性、高温動作時の着色、および高電圧動作時の着色を調べた。結果を表3に示す。
TFE/VdF/HFP(38/60/2モル%比)共重合体とTFE/VdF/HFP(6/77/17モル%比)共重合体ゴムを質量比で50/50でブレンドし、このブレンド物をTHFに溶解させ、参考例1で作製した正極に塗布し、80℃にて15分間乾燥させて、厚さ約2μmの電解液保持フィルム層で被覆された正極を作製した。この電解液保持フィルム被覆正極を用い、セパレータとしてポリエチレン製のセパレータ(厚さ22μm)を用いたほかは、参考例1同様の手法でラミネートセルを作製し、高温高電圧試験を行ったところ、正極での着色は観測されなかった。
参考例1において、電解液として、EC/ジメチルカーボネート(DMC)/EMC/HCF2CF2CH2OCF2CF2H(体積比20/50/10/20)にLiPF6を1M濃度で溶解した電解液に添加剤として、ビニレンカーボネート(VC)を0.1質量%、フルオロエチレンカーボネート(FEC)を3質量%加えた電解液を用い、セパレータとして電解液保持フィルム被覆セパレータ3を用いたほかは参考例1と同様にしてラミネートセルを作製し、つぎの条件で高温試験を行い、セパレータの着色の有無および容量維持率を調べた。結果を表4に示す。
つぎの充放電測定条件で60℃に保持し、100サイクル後の電解液保持フィルムの着色の有無、5サイクル目と比較した容量維持率を観察する。
充放電電圧:2.5~4.3V
充電:0.5C、4.3Vにて充電電流が1/10になるまで一定電圧を保持
放電:0.5C
実施例8において、電解液として、EC/DMC/EMC/HCF2CF2CH2OCF2CF2H(体積比20/50/10/20)にLiPF6を1M濃度で溶解した電解液に添加剤として、ビニレンカーボネート(VC)を0.1質量%、フルオロエチレンカーボネート(FEC)を3質量%加えた電解液を用い、セパレータとして電解液保持フィルムで被覆する前のポリエチレン製セパレータを用いたほかは実施例8と同様にしてラミネートセルを作製し、実施例8の高温試験を行い、セパレータの着色の有無および容量維持率を調べた。結果を表4に示す。
実施例8において、電解液として、EC/EMC(体積比30/70)にLiPF6を1M濃度で溶解した電解液を用いたほかは実施例8と同様にセパレータとして電解液保持フィルム被覆セパレータ3を用いてラミネートセルを作製し、実施例8の高温試験を行い、セパレータの着色の有無および容量維持率を調べた。結果を表4に示す。
実施例9において、セパレータとして電解液保持フィルムで被覆する前のポリエチレン製セパレータを用いたほかは実施例9と同様にしてラミネートセルを作製し、実施例8の高温試験を行い、セパレータの着色の有無および容量維持率を調べた。結果を表4に示す。
実施例8において、電解液保持フィルム被覆セパレータとして電解液保持フィルム被覆セパレータ6を用いたほかは実施例8と同様にしてラミネートセルを作製し、実施例8の高温試験を行い、セパレータの着色の有無および容量維持率を調べた。結果を表4に示す。
Claims (11)
- フッ化ビニリデン単位とテトラフルオロエチレン単位をフッ化ビニリデン単位/テトラフルオロエチレン単位がモル比で55/45~95/5で含み、かつヘキサフルオロプロピレン単位を0~10モル%含む(ただし、フッ化ビニリデン単位とテトラフルオロエチレン単位とヘキサフルオロプロピレン単位の合計量は100モル%である)フッ化ビニリデン系共重合体樹脂を含む電解液保持フィルムに非水電解液が含浸されてなる二次電池用ゲル電解質と、
ポリエチレン、ポリプロピレン及びポリイミドよりなる群から選ばれる少なくとも1種の樹脂からなる多孔質フィルムと、
からなる二次電池用ゲル電解質複合フィルム。 - フッ化ビニリデン系共重合体樹脂が、フッ化ビニリデン単位およびテトラフルオロエチレン単位のみからなるフッ化ビニリデン系2元共重合体樹脂である請求項1記載の二次電池用ゲル電解質複合フィルム。
- フッ化ビニリデン系共重合体樹脂が、ヘキサフルオロプロピレン単位を1~5モル%含むフッ化ビニリデン系3元共重合体樹脂である請求項1記載の二次電池用ゲル電解質複合フィルム。
- 電解液保持フィルムが、請求項1記載のフッ化ビニリデン系共重合体樹脂以外の他の樹脂および/またはゴムを含む請求項1~3のいずれかに記載の二次電池用ゲル電解質複合フィルム。
- 他の樹脂が、ポリアクリロニトリル、ポリアミドイミド、ポリフッ化ビニリデン、テトラフルオロエチレン/ヘキサフルオロプロピレン共重合体樹脂、またはこれらの2種以上の混合樹脂である請求項4記載の二次電池用ゲル電解質複合フィルム。
- 他のゴムが、フッ化ビニリデン/ヘキサフルオロプロピレン共重合体ゴム、フッ化ビニリデン/テトラフルオロエチレン/ヘキサフルオロプロピレン共重合体ゴム、アクリルゴム、またはこれらの2種以上の混合ゴムである請求項4記載の二次電池用ゲル電解質複合フィルム。
- 他の樹脂および/またはゴムの含有量が、請求項1記載のフッ化ビニリデン系共重合体樹脂100質量部に対して400質量部以下である請求項4記載の二次電池用ゲル電解質複合フィルム。
- 電解液保持フィルムが、金属酸化物粒子を含む請求項1~7のいずれかに記載の二次電池用ゲル電解質複合フィルム。
- 金属酸化物粒子が、酸化アルミニウム粒子または酸化ケイ素粒子である請求項8記載の二次電池用ゲル電解質複合フィルム。
- 金属酸化物粒子の平均粒子径が20μm以下である請求項8または9記載の二次電池用ゲル電解質複合フィルム。
- 請求項1~10のいずれかに記載の二次電池用ゲル電解質複合フィルムと電極を備える二次電池。
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WO2015049996A1 (ja) * | 2013-10-01 | 2015-04-09 | トヨタ自動車株式会社 | 二次電池 |
WO2015083790A1 (ja) | 2013-12-06 | 2015-06-11 | ダイキン工業株式会社 | 二次電池用セパレータ及び二次電池 |
JP2015216127A (ja) * | 2015-07-29 | 2015-12-03 | トヨタ自動車株式会社 | 二次電池 |
WO2017154449A1 (ja) * | 2016-03-10 | 2017-09-14 | 株式会社クレハ | ゲル状電解質およびその調製方法 |
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- 2011-02-07 CN CN2011800084105A patent/CN102754267A/zh active Pending
- 2011-02-07 KR KR1020127023095A patent/KR20120136355A/ko not_active Application Discontinuation
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WO2014065258A1 (ja) * | 2012-10-22 | 2014-05-01 | ダイキン工業株式会社 | セパレータ及び二次電池 |
JPWO2014065258A1 (ja) * | 2012-10-22 | 2016-09-08 | ダイキン工業株式会社 | セパレータ及び二次電池 |
WO2015049996A1 (ja) * | 2013-10-01 | 2015-04-09 | トヨタ自動車株式会社 | 二次電池 |
JP2015069967A (ja) * | 2013-10-01 | 2015-04-13 | トヨタ自動車株式会社 | 二次電池 |
WO2015083790A1 (ja) | 2013-12-06 | 2015-06-11 | ダイキン工業株式会社 | 二次電池用セパレータ及び二次電池 |
KR20160071440A (ko) | 2013-12-06 | 2016-06-21 | 다이킨 고교 가부시키가이샤 | 이차 전지용 세퍼레이터 및 이차 전지 |
JP2015216127A (ja) * | 2015-07-29 | 2015-12-03 | トヨタ自動車株式会社 | 二次電池 |
WO2017154449A1 (ja) * | 2016-03-10 | 2017-09-14 | 株式会社クレハ | ゲル状電解質およびその調製方法 |
WO2017154448A1 (ja) * | 2016-03-10 | 2017-09-14 | 株式会社クレハ | ゲル状電解質およびその調製方法 |
Also Published As
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KR20120136355A (ko) | 2012-12-18 |
JPWO2011096564A1 (ja) | 2013-06-13 |
US20120301794A1 (en) | 2012-11-29 |
CN102754267A (zh) | 2012-10-24 |
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