WO2005022674A1 - Battery separator and lithium secondary battery - Google Patents
Battery separator and lithium secondary battery Download PDFInfo
- Publication number
- WO2005022674A1 WO2005022674A1 PCT/JP2004/012499 JP2004012499W WO2005022674A1 WO 2005022674 A1 WO2005022674 A1 WO 2005022674A1 JP 2004012499 W JP2004012499 W JP 2004012499W WO 2005022674 A1 WO2005022674 A1 WO 2005022674A1
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- Prior art keywords
- separator
- battery
- porous
- lithium secondary
- linear
- Prior art date
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Classifications
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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
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
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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
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/411—Organic material
- H01M50/414—Synthetic resins, e.g. thermoplastics or thermosetting resins
- H01M50/417—Polyolefins
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/449—Separators, membranes or diaphragms characterised by the material having a layered structure
- H01M50/457—Separators, membranes or diaphragms characterised by the material having a layered structure comprising three or more layers
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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
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/463—Separators, membranes or diaphragms characterised by their shape
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/443—Particulate material
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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
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/489—Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
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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
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/489—Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
- H01M50/491—Porosity
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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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Definitions
- the present invention relates to a battery separator and a lithium secondary battery.
- a lithium battery usually has a configuration in which a positive electrode, a negative electrode, a separator, and a non-aqueous electrolyte are accommodated in a cylindrical, square, or disk-shaped container.
- a positive electrode a positive electrode mainly composed of a lithium composite oxide such as LiCo O is used, and as the negative electrode, a carbon material or
- a negative electrode made of lithium metal is generally used.
- a porous film formed of polyolefin such as polyethylene (PE) or polypropylene (PP), or a porous film formed of a single porous polyethylene film on both sides.
- PE polyethylene
- PP polypropylene
- a laminated porous film having a configuration in which porous polypropylene films are laminated is used.
- a positive electrode sheet, a negative electrode sheet, and a separator are overlapped and spirally wound using a metal winding pin to form a battery element (
- a wound product is prepared, the wound product is stored in a battery container, and then a non-aqueous electrolyte is injected to manufacture a battery.
- lithium secondary batteries have become increasingly high capacity.
- a method of increasing the capacity a method of increasing the volume occupied by the electrode active material in a limited size battery container and decreasing the volume occupied by other members to achieve a high capacity is generally employed.
- the density of the electrode mixture containing the electrode active material gradually increases, and the thickness of the electrode mixture gradually increases, while the thickness of the current collector and the separator of the electrode mixture must be gradually reduced. It is now. For this reason, the remaining space becomes extremely small, so that it is difficult to inject the nonaqueous electrolyte into the container, and it takes time to inject the nonaqueous electrolyte. Furthermore, it tends to be difficult to uniformly impregnate the non-aqueous electrolyte into the separator after injection.
- Patent Document 1 discloses that a separator and an electrode seal are formed by roughening the surface of the separator. There is disclosed an invention for facilitating the injection of a non-aqueous electrolyte into a battery container in which a rolled product containing a roll containing a separator and a plurality of grooves extending in the width direction of the separator along with the surface roughening. Is also described.
- Patent Document 1 JP-A-6-333550
- a plurality of nonporous linear regions extending in the width direction are formed on a long porous film, and at least one surface of the nonporous linear regions forms a concave portion or a convex portion.
- Battery separator is not limited to
- the present invention also provides a lithium secondary battery including a positive electrode, a negative electrode, a separator, and a non-aqueous electrolyte, wherein the separator is the separator of the present invention.
- At least one end of the non-porous linear region of the separator extends from the side surface of the separator.
- the non-aqueous electrolyte of the lithium secondary battery contains at least one compound selected from a cyclic carbonate, a chain carbonate, a chain ester, and ratatone.
- the non-aqueous electrolyte of the lithium secondary battery contains at least one compound selected from vinylene carbonate, dimethyl vinylene carbonate, butyl ethylene carbonate, high-angle calactone, and divinyl sultone.
- the separator of the present invention when used as a separator, the non-aqueous electrolyte is injected into a battery container containing a wound product including the separator and the electrode sheet. Therefore, the injection time is shortened, and the uniformity of permeation of the nonaqueous electrolyte into the container after the injection is improved. Therefore, when the battery is a secondary battery, the cycle characteristics of the battery are improved as well as the workability of the battery production. Furthermore, since the mechanical strength and dimensional stability of the separator are improved, a short circuit is less likely to occur, and the effect of preventing overcharging also appears.
- FIG. 1 is a partial cross-sectional view of an example of a battery separator according to the present invention, which has a nonporous region and the surface of the nonporous region is a concave portion.
- the separator in FIG. 1 has a configuration in which a porous polypropylene layer 1, a porous polyethylene layer 2, and a porous polypropylene layer 3 are laminated and bonded, and as a whole, a porous region 5 and a nonporous region 6 are formed.
- the concave portion 4a is formed on the surface of the non-porous region.
- FIG. 2 shows a partial cross-sectional view of a battery separator having a non-porous region of the present invention, and the surface of the non-porous region is a projection.
- the separator in FIG. 2 has a configuration in which a porous polypropylene layer 1, a porous polyethylene layer 2, and a porous polypropylene layer 3 are laminated and bonded, and as a whole, a porous region 5 and a non-porous region 6 are formed.
- the convex portion 4b is formed on the surface of the non-porous region.
- FIG. 3 to FIG. 11 show various examples of the concave or convex pattern on the surface of the battery separator of the present invention.
- the concave portion or the convex portion has a linear shape extending entirely along the width of the separator.
- the concave portion or the convex portion has a V-shape that is symmetrical with respect to a center line along the length direction of the separator.
- the concave portions or convex portions are in the form of oblique lattices extending entirely along the width of the separator.
- the concave portion or the convex portion has an S-shape extending entirely along the width of the separator.
- the concave portions and the convex portions alternately extend in a linear shape along the width of the separator.
- FIG. 8 shows a shape in which the concave portion has a linear shape extending entirely along the width of the separator, and a linear convex portion extending in the length direction of the separator is additionally provided.
- FIG. 9 shows a shape in which the concave portion has a linear shape extending entirely along the width of the separator, and a linear convex portion extending in an oblique direction is additionally provided.
- FIG. 10 shows a V-shaped shape in which the concave portion is symmetrical with respect to a center line along the length direction of the separator, and shows a shape in which a circular convex portion is additionally provided.
- FIG. 11 shows a shape in which the concave portion has a linear shape extending entirely along the width of the separator, and the dot-shaped convex portions are dispersed and formed.
- the porous film that can be used for the separator of the present invention is a porous film having a large number of penetrating micropores.
- the porous film that serves as a separator has a high ion permeability, has a predetermined mechanical strength, and is good as long as it is an insulating thin film.
- the material include an olefin polymer, a fluorine polymer, a senorelose polymer, and a polyimide. , Polyamide (Ni-Nippon) and glass fiber are used.
- a nonwoven fabric, a woven fabric, or a microporous film is used as a form.
- Particularly preferred materials are polypropylene, polyethylene, a mixture of polypropylene and polyethylene, and a mixture of polypropylene and polyperfluoroethylene.
- a single-layer porous film of polypropylene or polyethylene and polypropylene and polyethylene Any structure of the laminated porous film which is a mixture of the components may be used.
- the method for making the porous film porous may be a drawing method (dry method) or an extraction method (wet method).
- the nonporous concave portion of the bottom of the separator of the present invention is continuous in a direction of 90 ⁇ 10 degrees with respect to the longitudinal direction of the battery separator, and has a density of 0.1 / cm.
- the above is preferable 0.3 Zcm or more is more preferable 0.5 Zcm or more is most preferable.
- 10 lines / cm or less is preferable 5 lines / cm or less is more preferable 3 lines Zcm or less is most preferable
- the depth of the recess separator having the present invention 2 xm or preferably Ri good more preferably tool is instrument 4 or M m is most preferable. Meanwhile, most preferably at most 10 xm less preferred instrument 9 M m or less good Ri preferred tool 8 xm.
- the width of the concave portion of the separator of the present invention is preferably 3 ⁇ m or more, more preferably 5 ⁇ m or more, and most preferably 10 ⁇ or more.
- the width of the concave portion is preferably 500 ⁇ 500 ⁇ or less, more preferably 300 ⁇ m or less, most preferably 200 ⁇ m or less.
- the recess may be formed on both sides of the battery separator, which is preferably formed on at least one side.
- concave portions or convex portions
- the concave portion of the battery separator works smoothly as a gas release path, so that the concave portion of the battery separator is Preferably.
- thermocompression bonding between nip rolls is preferable.
- the porous film is formed at a melting point of the material of ⁇ 80 ° C, more preferably ⁇ 30. 0. 1-10kgZcm 2 between heated rolls adjusted to a temperature range and C, more preferably dividing lines by crimping at a nip pressure of 1 one 3 kg / cm 2.
- the concave portions can be provided to the separator either before or after making it porous by a stretching method (dry method) or by an extraction method (wet method), but more preferably after making it porous.
- a stretching method dry method
- an extraction method wet method
- the film is uniaxially or The film is biaxially stretched to optimize the film thickness, porosity, or porous structure.
- the provision of the concave portion on the battery separator can be performed before or after the uniaxial stretching or the biaxial stretching.
- the stretching method since the film is uniaxially stretched in the longitudinal direction to make the film porous, it is preferable that the concave portion is provided after the film separator is stretched so that the dimensional change in the width direction of the battery separator hardly occurs.
- the extraction method wet method
- biaxial stretching in which the film is stretched not only in the longitudinal direction but also in the width direction is performed, but it is preferable to provide a concave portion before performing the biaxial stretching.
- the separator is provided with a convex portion having a non-porous region force continuous in a direction substantially intersecting the longitudinal direction of the porous film.
- the protrusions provided on the porous film are continuous in the direction of 90 ⁇ 30 degrees with respect to the longitudinal direction of the separator, and the density is preferably 0.1 / cm or more. Zcm or more is more preferable 0.5 line Zcm or more is most preferable. On the other hand, 10 / cm or less is preferred, 5 / cm or less is more preferred, and 3 / cm or less is most preferred.
- the height of the projection provided on the separator is preferably 2 ⁇ or more, more preferably 3 ⁇ or more, and most preferably 4 / im or more.
- the force S is preferably 20 ⁇ or less, more preferably 15 / im or less, most preferably 10 ⁇ or less.
- the width of the protrusion provided on the separator is preferably 3 ⁇ m or more, more preferably 5 ⁇ m or more, and most preferably 10 m or more.
- the force S is preferably 500 m or less, more preferably 200 ⁇ or less, which is more preferable than the force S of 300 m or less.
- the protrusions provided to the separator may be formed on at least one surface of the porous film, which is preferably formed on at least one surface.
- the convex portion of the battery separator works smoothly as a gas release path, so that the convex portion of the battery separator is positive. Les, preferably facing the side.
- the form may be maintained as it is after the injection, or may be dissolved in a non-aqueous electrolyte to make the form disappear.
- polypropylene, polyethylene, ethylene- A film or filler having a predetermined thickness made of a material selected from the group consisting of copolymer, polybutene 1, propylene butene 1 copolymer, polyimide, and cellulose can be bonded to a battery separator by thermocompression bonding. .
- the material for forming the projections may be polyethylene oxide, polyvinylidene fluoride, polyacrylonitrile, polystyrene, or the like.
- Polymer materials and copolymers of the above high molecular materials such as ethylene-methacrylic acid copolymer, ethylene-acrylic ester copolymer, and styrene-butadiene copolymer can be used. These materials can lose their form by dissolving in a non-aqueous electrolyte after battery assembly. Further, the melting of the protrusions leads to a reduction in the tightening tension of the battery element after the battery is assembled, so that an effect of preventing damage to the film due to the tightening can be expected.
- the concave portion and the convex portion may be a single continuous line or point continuum as long as the nonaqueous electrolyte can be guided in a direction substantially intersecting with the longitudinal direction of the separator. It is preferably at least one kind of continuum of the line segment.
- These linear structures are preferably shaped so as to be symmetrical when the separator is folded back at its center line along its longitudinal direction, especially linear, grid-shaped, diagonal grid-shaped, V-shaped. More preferably, it has a continuous structure such as a letter shape, a W shape, or an S shape.
- FIGS. 3 to 6 are schematic plan views of linear, V-shaped, lattice-shaped, and S-shaped patterns in the case where concave portions or convex portions are formed in the separator.
- FIG. 7 shows a schematic plan view of a pattern of a combination structure (type) of a concave portion and a convex portion of a linear alternating type.
- the solid line portion indicates a concave portion
- the broken line portion indicates a convex portion.
- the structure of the concave portion and the convex portion is required.
- a concave portion or a convex portion having a form selected from a linear shape, a circular shape, and a polygonal shape.
- Figures 8 to 10 show schematic plan views of the additional type combination structure (type) of concave and convex portions, with additional linear line segments, additional linear line segments (rhombic), and additional V-shaped circles. Shown in The solid line in the figure indicates a concave portion, and the broken line indicates a convex portion.
- the air permeability of the battery separator manufactured as described above is preferably 30 seconds or more and more preferably 50 seconds or more and more preferably 100 seconds or more.
- 1000 sec / l OOcc or less is preferable, and 900 sec / l OOcc or less is more preferable. 800 sec / l OOcc or less is most preferable.
- the maximum pore diameter is 0.02-3 ⁇ m, and more preferably, the porosity is 30-85%, since the capacity characteristics of the battery are improved.
- the thickness of the battery separator is preferably 5 / im or more in terms of mechanical strength and performance, more preferably 8 ⁇ or more, most preferably ⁇ ⁇ or more.
- 100 ⁇ or less is preferred, and 40 / im or less is more preferred, and 30 ⁇ m or less is most preferably prepared.
- the constituent members other than the separator in the lithium secondary battery of the present invention are not particularly limited, and various constituent members of a conventionally used lithium secondary battery can be used.
- Ratatotones (GBL) ratatones such as ⁇ -valerolatatatone, dimethyl carbonate (DMC), methyl ethyl carbonate (MEC), getyl carbonate (DEC), methyl propyl carbonate, dipropyl carbonate, methyl butyl carbonate, dibutyl carbonate, etc.
- Chain carbonates tetrahydrofuran, 2-methyltetrahydrofuran, 1,4-dioxane, 1,2-dimethoxyethane, 1,2-di Ethers such as ethoxyxetane and 1,2-dibutoxetane, nitriles such as acetonitrile and adiponitrile, phosphates such as trimethyl phosphate and trioctyl phosphate, butyl formate, methyl propionate, methyl bivalate, and butyl bivalate
- Non-aqueous solvents such as chain esters such as octyl bivalate and amides such as dimethylformamide are used.
- the non-aqueous solvents it is preferable that at least one selected from cyclic carbonates, ratatones, chain carbonates and chain esters is contained.
- non-aqueous solvents are usually used as a mixture in order to achieve appropriate physical properties.
- the combination include a combination of a cyclic carbonate and a chain carbonate, a combination of a cyclic carbonate and a ratatone, a combination of a rataton and a chain ester, a combination of a cyclic carbonate, a ratatone and a chain ester.
- Various combinations such as a combination of linear carbonates and chain esters are possible, and the mixing ratio is not particularly limited. It is preferable to include at least one of cyclic carbonates and chain carbonates in the non-aqueous solvent. Particularly, when the cyclic carbonates and chain carbonates are contained in combination, the cycle characteristics are excellent and the capacity is high. This is preferable because a battery can be provided.
- the ratio of the cyclic carbonates to the chain carbonates is preferably 20:80 to 40:60 force S, particularly preferably 25:75 to 35:65 force S in terms of volume ratio.
- asymmetric carbonates such as methinoleethynolecarbonate, methinolepropynolecarbonate and methinolebutynolecarbonate.
- methyl carbonate which is an asymmetric chain carbonate which is a liquid at a low temperature and has a relatively high boiling point and thus little evaporation.
- At least one selected from double bond-containing compounds such as vinylene carbonate (VC), dimethyl vinylene carbonate, butyl ethylene carbonate, triangular lactone, and divinyl sulfone is added to these non-aqueous solvents. Is preferred.
- a high-capacity battery has a high electrode mixture density, and thus has a poor liquid injection property and a low cycle characteristic.
- the content of the double bond-containing compound is excessively large, the battery performance may be degraded, and if the content is excessively small, sufficient expected battery performance cannot be obtained. Accordingly, 0.01% by weight or more is preferable, 0.1% by weight or more is more preferable, and 0.5% by weight or more is most preferable, based on the total weight of the nonaqueous electrolyte. On the other hand, 10% by weight or less is preferred, 7% by weight or less is more preferred, and 5% by weight or less is most preferred.
- cyclohexynolebenzene fluorocyclohexylbenzene compounds (1-fluoro-2-cyclohexylbenzene, 1_fluoro-3-cyclohexylbenzene, 1_fluoro-4-cyclohexyl) Benzene), biphenyl, terphenyl (o_ form, m-form, p-form), diphenyl ether, 2-fluorodiphenyl ether, 4-diphenyl ether, fluorobenzene, difluorene benzene (o— Body, m-body, ⁇ -body), 2_fluorobiphenyl, 4_fluorobiphenyl, 2,4-difluoroanisole, 2,5-difluoroanisole, 2,6-diflu Oroanisone, tert-but
- a cyclohexynolebenzene skeleton, a diphenyl skeleton, or a fluorine-substituted aromatic compound is preferable.
- the content of the aromatic compound is excessively large, the battery performance may be degraded, and if the content is excessively small, the expected safety cannot be obtained. Therefore, 0.1% by weight or more is preferable, 0.5% by weight or more is more preferable, and 1% by weight or more is most preferable with respect to the total weight of the nonaqueous electrolyte. On the other hand, 10% by weight or less is preferred, 7% by weight or less is more preferred, and 5% by weight or less is most preferred.
- the cycle characteristics and the safety are further improved. Preferred, because we can provide lithium secondary batteries.
- Examples of the electrolyte used in the present invention include LiPF, LiBF, LiCIO, CF SO Li, and the like. LiN (SO CF), LiN (SO C F), LiC (SO CF), LiPF
- CF LiPF (CF), LiPF (CF), LiPF (iso_CF), LiPF (iso-CF) and other lithium salts containing a chain alkyl group, (CF) (SO) NLi, ( CF) (SO) N
- Lithium salts containing a cyclic alkylene chain such as Li are mentioned. These electrolyte salts may be used alone or in combination of two or more. These electrolysis The quality is preferably 0.1 M or more with respect to the above non-aqueous solvent, and more preferably 0.5 M or more.
- the electrolytic solution of the present invention can be obtained, for example, by mixing the above-mentioned non-aqueous solvent and dissolving the above-mentioned electrolyte salt therein.
- air or carbon dioxide in the battery of the present invention, for example, it is possible to suppress the generation of gas due to the decomposition of the electrolyte and to improve the battery performance such as cycle characteristics and storage characteristics. it can.
- the method of containing (dissolving) carbon dioxide or air in the non-aqueous electrolyte includes (1) air or carbon dioxide before the non-aqueous electrolyte is injected into the battery in advance.
- Air or carbon dioxide-containing gas can be contained in the battery either after injection or before or after battery sealing, or a combination of these methods. it can. Air and carbon dioxide-containing gas containing as little moisture as possible have a preferred dew point of 40 ° C or less, and particularly preferably a dew point of 50 ° C or less.
- the entire amount of the electrolytic solution may be injected into the battery of the present invention at one time, but it is preferably performed in two or more steps. Also, it is preferable to reduce the pressure (preferably 500 to 1 tonole, more preferably 400 to 10 torr) or pressurize the battery can to shorten the electrolyte injection time. May be performed.
- oxides such as MnO and VO, or cobalt, manganese, and nickel oxide are used.
- lithium composite oxide with nickel containing nickel is used.
- One of these positive electrode active materials may be selected and used, or two or more thereof may be used in combination.
- Such lithium composite oxides include, for example, LiCoO, LiMnO, LiNi
- LiCoNiO (0.01 ⁇ x ⁇ l), LiMnNiCo ⁇ and the like. Also, LiC
- a lithium composite oxide having an open circuit voltage of 4.3 V or more on the Li basis after charging as described above is most preferable, and a lithium composite oxide containing Co or Ni is most preferable.
- a part of the lithium composite oxide may be replaced by another element
- the battery separator of the present invention has a great effect in a lithium battery using a positive electrode active material suitable for high voltage and high energy density.
- the conductive agent for the positive electrode may be any electronic conductive material that does not cause a chemical change.
- Examples include graphites such as natural graphite (flaky graphite and the like) and artificial graphite, and carbon blacks such as acetylene black, ketjen black, channel black, furnace black, lamp black and thermal black. It is also acceptable to use a mixture of graphite and carbon black as appropriate.
- the amount of the conductive agent to be added to the positive electrode mixture is preferably 11 to 10% by weight, and particularly preferably 25% by weight.
- the positive electrode comprises the above-mentioned positive electrode active material, a conductive agent such as acetylene black or carbon black, polytetrafluoroethylene (PTFE), polyvinylidene fluoride (PVDF), a copolymer of styrene and butadiene (SBR), After kneading with a binder such as copolymer of acrylonitrile and butadiene (NBR) and propyloxymethylcellulose (CMC) to form a positive electrode mixture, this positive electrode material is made of aluminum foil as a current collector and stainless steel lath. It is prepared by applying it to a plate, drying, pressing, and then heating it under vacuum at a temperature of about 50 ° C to 250 ° C for about 2 hours.
- a conductive agent such as acetylene black or carbon black
- PTFE polytetrafluoroethylene
- PVDF polyvinylidene fluoride
- SBR copolymer of styrene
- the negative electrode As the negative electrode (negative electrode active material), a material capable of occluding and releasing lithium is used.
- lithium metal lithium alloy (eg, Al, Sn, Zn, alloy of Si and lithium), tin Tin compounds, silicon, silicon compounds and carbon materials (pyrolyzed carbons, coatas, dalaphites (artificial graphite, natural graphite, etc.), organic polymer compound burners, carbon fibers) are used.
- the lattice spacing (d) of the lattice plane (002) is preferably 0.340 nm or less.
- the graphite crystal structure having a graphite crystal structure of 0.335-0.337 nm is preferred.
- One of these negative electrode active materials may be selected and used, or two or more thereof may be used in combination.
- powder materials such as carbon material ethylene propylene diene terpolymer (EPDM), polytetrafluoroethylene (PTFE), polyvinylidene fluoride (PVDF), copolymer of styrene and butadiene (SBR), acrylonitrile and butadiene Copolymer (NBR), power It is used as a negative electrode mixture by kneading with a binder such as ropoxymethylcellulose (CMC).
- the method for manufacturing the negative electrode is not particularly limited, and the negative electrode can be manufactured by the same method as the above-described method for manufacturing the positive electrode.
- the density of the positive electrode mixture layer formed on the aluminum foil is preferably 3.2-4. OgZcm 3, more preferably 3.3-3.9 g / cm 3 , and most preferably 3.4-3. 8 g / cm 3 .
- the density of the positive electrode mixture exceeds 4. Og / cm 3 , the production becomes substantially difficult.
- the density of the negative electrode mixture layer formed on the copper foil is 1.3-2. Og / cm 3 , more preferably 1.4-1.9 gZcm 3 , and most preferably 1.5-1.8 g / cm 3 . it is between cm 3.
- the preferable thickness of the positive electrode layer is 30 to 120 ⁇ m, preferably 50 to 100 ⁇ m, and the thickness of the negative electrode layer (Per one side of the current collector) is 100 ⁇ m, preferably 370 ⁇ m.
- the lithium secondary battery of the present invention has excellent cycle characteristics over a long period of time even when the end-of-charge voltage is higher than 4.2V, and particularly when the end-of-charge voltage is 4.3V. It also has excellent cycle characteristics.
- the discharge end voltage can be 2.5 V or more, and further 2.8 V or more.
- the current value is not particularly limited, it is usually used in a constant current discharge of 0.1 to 3C.
- the lithium secondary battery of the present invention has a power capable of charging and discharging in a wide range of -40 to 100 ° C, preferably 0 to 80 ° C.
- a safety valve can be used for the sealing plate.
- a method of making a cut in a member such as a battery can or a gasket can also be used.
- various conventionally known safety elements at least one of a fuse, a bimetal, and a PTC element as an overcurrent prevention element. It is preferable to use these overcurrent prevention elements together with the shutdown function of the battery separator because safety is greatly improved.
- a plurality of lithium secondary batteries according to the present invention are assembled in series and Z or in parallel as needed, and stored in a battery pack.
- the battery pack contains safety elements such as PTC elements, thermal fuses, fuses and / or current cutoff elements, as well as safety circuits (each battery and / or Alternatively, a circuit having a function of monitoring the voltage, temperature, current, etc. of the entire assembled battery and interrupting the current may be provided.
- the battery of the present invention can be used for various devices.
- it is preferably used for mobile phones, notebook computers, PDAs, video movies, compact cameras, razors, electric tools, automobiles and the like.
- the lithium secondary battery of the present invention is preferable because of its high reliability.
- the three-layer structure consisting of a polypropylene (PP) layer / polyethylene (PE) layer / polypropylene (PP) layer is thermocompression-bonded to an embossing roll heated to 130 ° C.
- a linear concave portion having a nonporous bottom was formed continuously in a direction at 90 degrees to the longitudinal direction of the porous long laminated film.
- the densities of the recesses are 0.2 lines / lcm with respect to the longitudinal direction of the porous long laminated film, the average depth is 8 ⁇ m, the average width is 200 ⁇ m, and the film thickness is The air permeability was 25.7 ⁇ m, the air permeability was 530 sec / 100 cc, the maximum pore diameter was 0, and the porosity was 41%.
- the separator was overlapped with a 22-zm-thick aluminum foil and wound into a cylindrical shape to produce a pseudo battery element.
- the size of the pseudo battery element was 9.5 mm ⁇ (outer diameter) X 60 mm (height) cylindrical.
- This pseudo battery element was immersed in a non-aqueous electrolyte prepared by dissolving LiPF into 1MZL in a 1: 1 (volZvol) mixed solution of getyl carbonate / propylene carbonate for a specified time, and the weight before and after immersion was measured. did.
- Figure 12 shows the non-aqueous electrolyte absorption rate (weight change).
- VC vinylene carbonate
- PS 1,3-propane sultone
- CHB cyclohexylbenzene
- LiCoO positive electrode active material
- acetylene black conductive agent
- polyvinylidene fluoride binder
- An 18650-size cylindrical battery (diameter 18 mm, height 65 mm) was fabricated.
- the battery was provided with a pressure release port and an internal current interrupt device (PTC element).
- the electrode density of the positive electrode was 3.5 g / cm 3
- the electrode density of the negative electrode was 1.6 g / cm 3 .
- the thickness of the positive electrode layer (per one side of the current collector) was 70 ⁇ m
- the thickness of the negative electrode layer (per one side of the current collector) was 60 ⁇ m.
- the above 18650 battery was charged at a constant current of 2.2A (1C) up to 4.2V at a high temperature (45 ° C), and then charged at a constant voltage of 4.2V for a total of 3 hours under a constant voltage. Next, under a constant current of 2.2 A (1 C), the battery was discharged to a final voltage of 2.8 V, and this charge / discharge was repeated.
- the initial discharge capacity was almost the same as that of the battery of Comparative Example 1 below. When the battery characteristics after 200 cycles were measured, the discharge capacity retention rate when the initial discharge capacity was 100% was 83.1%. Was.
- Example 1 Except that the porous long laminated film having a three-layer structure of the polypropylene (PP) layer / polyethylene (PE) layer / polypropylene (PP) layer used in Example 1 was used as it was as a separator, In the same manner as in Example 1, the absorption rate (weight change) of the nonaqueous electrolyte was measured. The results are shown in FIG.
- Example 2 Using the above separator, a lithium secondary battery was prepared in the same manner as in Example 1, and the battery characteristics after 200 cycles were measured. The discharge capacity was maintained when the initial discharge capacity was 100%. The rate was 75.7%. When an overcharge test was performed in the same manner as in Example 1, the surface temperature of the battery exceeded 120 ° C. and generated heat.
- Polypropylene (PP) layer Polyethylene filler is thermocompression-bonded to a porous long laminated film consisting of a three-layer structure of Z polyethylene (PE) layer / polypropylene (PP) layer to form a porous length.
- the laminated film having a cross-section shown in FIG. 2 and having a plurality of non-porous convex regions having the shape shown in FIG. 3 was obtained.
- the density of the protrusions was 0.2 lines / lcm with respect to the longitudinal direction of the separator, the average height was 15 / im, and the average width was 25 / im.
- a lithium secondary battery was prepared using the above separator in the same manner as in Example 1, and the battery characteristics after 200 cycles were measured. The discharge capacity was maintained when the initial discharge capacity was set to 100%. The rate was 82.6%. When an overcharge test was performed in the same manner as in Example 1, the surface temperature of the battery was 120 ° C. or lower.
- Polypropylene (PP) layer A porous long laminated film consisting of a three-layer structure of a Z polyethylene (PE) layer / polypropylene (PP) layer, the shape of which is shown in FIG. A plurality of non-porous regions of the concave portion having a cross section shown in FIG. 1 having such an oblique lattice shape were formed to obtain a separator according to the present invention.
- the nonaqueous electrolyte solution absorption rate (weight change) was measured in the same manner as in Example 1 except that the above separator was used.
- Fig. 14 shows the results.
- a lithium secondary battery was prepared using the above separator in the same manner as in Example 1, and the battery characteristics after 200 cycles were measured. The discharge capacity was maintained when the initial discharge capacity was set to 100%. The rate was 81.9%. When an overcharge test was performed in the same manner as in Example 1, the surface temperature of the battery was 120 ° C. or lower.
- Example 3 The procedure was performed except that the porous long laminated film having a three-layer structure of the polypropylene (PP) layer / polyethylene (PE) layer / polypropylene (PP) layer used in Example 3 was used as a separator. In the same manner as in Example 1, the non-aqueous electrolyte solution absorption rate (weight change) was measured. Fig. 14 shows the results.
- FIG. 1 shows a partial cross-sectional view of an example of a battery separator of the present invention.
- FIG. 2 shows a partial cross-sectional view of another example of the battery separator of the present invention.
- FIG. 3 shows an example of a concave or convex pattern on the surface of the battery separator of the present invention.
- FIG. 4 shows another example of a pattern of concave portions or convex portions on the surface of the battery separator of the present invention.
- FIG. 5 shows another example of a concave or convex pattern on the surface of the battery separator of the present invention.
- FIG. 6 shows another example of a concave or convex pattern on the surface of the battery separator of the present invention.
- FIG. 7 shows another example of a pattern of concave portions or convex portions on the surface of the battery separator of the present invention.
- FIG. 8 shows another example of a pattern of concave portions or convex portions on the surface of the battery separator of the present invention.
- FIG. 9 shows another example of a pattern of concave portions or convex portions on the surface of the battery separator of the present invention.
- FIG. 10 shows another example of a concave or convex pattern on the surface of the battery separator of the present invention.
- FIG. 11 shows another example of a pattern of concave portions or convex portions on the surface of the battery separator of the present invention.
- FIG. 12 shows the production of a lithium secondary battery using the battery separator of the present invention of Example 1 and the production of a lithium secondary battery using the separator of Comparative Example 1 having no concave or convex portions formed.
- FIG. 4 is a diagram showing a change in an absorption rate of a non-aqueous electrolyte.
- FIG. 13 shows the production of a lithium secondary battery using the battery separator of the present invention of Example 2 and the production of a lithium secondary battery using the separator of Comparative Example 1 in which no concave portion or convex portion was formed. It is a figure showing change of the absorption rate of a nonaqueous electrolyte.
- FIG. 14 shows the production of a lithium secondary battery using the battery separator of the present invention in Example 3, the formation of a concave portion or a convex portion, and the use of a lithium secondary battery using the separator of Comparative Example 2. It is a figure which shows the change of the absorption rate of the nonaqueous electrolyte solution of battery manufacture.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Inorganic Chemistry (AREA)
- Secondary Cells (AREA)
- Cell Separators (AREA)
Abstract
Description
Claims
Priority Applications (2)
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US10/569,971 US7595130B2 (en) | 2003-11-06 | 2004-08-30 | Battery separator and lithium secondary battery |
JP2005513501A JP4529903B2 (en) | 2003-08-29 | 2004-08-30 | Battery separator and lithium secondary battery |
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JP2003-306354 | 2003-08-29 | ||
JP2003-306355 | 2003-08-29 | ||
JP2003306354 | 2003-08-29 | ||
JP2003306355 | 2003-08-29 | ||
JP2003426650 | 2003-12-24 | ||
JP2003-426651 | 2003-12-24 | ||
JP2003426651 | 2003-12-24 | ||
JP2003-426650 | 2003-12-24 |
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WO2005022674A1 true WO2005022674A1 (en) | 2005-03-10 |
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PCT/JP2004/012499 WO2005022674A1 (en) | 2003-08-29 | 2004-08-30 | Battery separator and lithium secondary battery |
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JP (1) | JP4529903B2 (en) |
KR (1) | KR100977433B1 (en) |
WO (1) | WO2005022674A1 (en) |
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Also Published As
Publication number | Publication date |
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KR20060132556A (en) | 2006-12-21 |
KR100977433B1 (en) | 2010-08-24 |
JPWO2005022674A1 (en) | 2007-11-01 |
JP4529903B2 (en) | 2010-08-25 |
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