WO2021085946A1 - 음극 활물질의 제조 방법, 음극 활물질, 이를 포함하는 음극, 및 상기 음극을 포함하는 이차 전지 - Google Patents
음극 활물질의 제조 방법, 음극 활물질, 이를 포함하는 음극, 및 상기 음극을 포함하는 이차 전지 Download PDFInfo
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- WO2021085946A1 WO2021085946A1 PCT/KR2020/014567 KR2020014567W WO2021085946A1 WO 2021085946 A1 WO2021085946 A1 WO 2021085946A1 KR 2020014567 W KR2020014567 W KR 2020014567W WO 2021085946 A1 WO2021085946 A1 WO 2021085946A1
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- H—ELECTRICITY
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- 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
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
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- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/05—Preparation or purification of carbon not covered by groups C01B32/15, C01B32/20, C01B32/25, C01B32/30
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- C01B32/20—Graphite
- C01B32/21—After-treatment
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- H01M10/052—Li-accumulators
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- H01M4/04—Processes of manufacture in general
- H01M4/0471—Processes of manufacture in general involving thermal treatment, e.g. firing, sintering, backing particulate active material, thermal decomposition, pyrolysis
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- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/133—Electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
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- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/139—Processes of manufacture
- H01M4/1393—Processes of manufacture of electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
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- H01M4/36—Selection of substances as active materials, active masses, active liquids
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- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/362—Composites
- H01M4/366—Composites as layered products
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- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
- H01M4/583—Carbonaceous material, e.g. graphite-intercalation compounds or CFx
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- H—ELECTRICITY
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- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
- H01M4/583—Carbonaceous material, e.g. graphite-intercalation compounds or CFx
- H01M4/587—Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
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- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
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- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/624—Electric conductive fillers
- H01M4/625—Carbon or graphite
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/30—Particle morphology extending in three dimensions
- C01P2004/32—Spheres
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- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/60—Particles characterised by their size
- C01P2004/61—Micrometer sized, i.e. from 1-100 micrometer
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- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/80—Particles consisting of a mixture of two or more inorganic phases
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- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/12—Surface area
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- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/14—Pore volume
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/40—Electric properties
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- H—ELECTRICITY
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- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M2004/021—Physical characteristics, e.g. porosity, surface area
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- H—ELECTRICITY
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- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
- H01M2004/027—Negative electrodes
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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 comprises the steps of forming composite particles by mixing a carbonaceous core and pitch and performing a first heat treatment; And mixing the composite particles and the pitch and performing a second heat treatment; a method for preparing a negative active material, a negative active material, a negative electrode, and a secondary battery.
- a rechargeable battery is a representative example of an electrochemical device that uses such electrochemical energy, and its use area is gradually expanding.
- a secondary battery is composed of a positive electrode, a negative electrode, an electrolyte, and a separator.
- the negative electrode may include a negative electrode active material that inserts and desorbs lithium ions from the positive electrode, and a binder that imparts adhesion so that the negative electrode active material is not separated from the negative electrode.
- styrene butadiene rubber SBR is mainly used as a binder.
- the SBR is a point binder and serves to impart adhesion (negative electrode adhesion) between the negative electrode active material and/or the negative electrode active material and the current collector.
- a carbonaceous material such as graphite may be used as the negative active material.
- a carbonaceous material such as graphite
- since a large number of large pores are formed on the surface there is a problem that the adhesion area between the SBR and the carbonaceous material is reduced, and thus the ability to impart adhesion of the SBR is reduced.
- there is a method of forming a functional group including oxygen or the like on the surface of the carbonaceous material but this leads to a decrease in the capacity of the carbonaceous material.
- the present invention proposes a new method for improving negative electrode adhesion by reducing a large number of large pores existing on the surface of a carbonaceous material.
- One problem to be solved by the present invention is to provide a method of manufacturing a negative electrode active material and a negative electrode active material capable of improving negative electrode adhesion.
- Another problem to be solved by the present invention is to provide a negative electrode and a secondary battery including the negative electrode active material.
- a negative active material comprising a carbonaceous core and a carbon coating layer and having a total pore volume of 0.003cm 3 /g to 0.010cm 3 /g is provided.
- a negative electrode including the negative active material is provided.
- a secondary battery including the negative electrode is provided.
- the total pore volume of the negative active material may be reduced. Accordingly, the adhesion between the negative active material and the binder may be strengthened, so that the negative electrode adhesion may be improved, and life characteristics of the battery may be improved.
- D 50 may be defined as a particle diameter corresponding to 50% of the cumulative volume in the particle size distribution curve (graph curve of the particle size distribution diagram) of each particle.
- the D 50 may be measured using, for example, a laser diffraction method.
- the laser diffraction method can measure a particle diameter of about several mm from a submicron region, and high reproducibility and high resolution results can be obtained.
- the BET specific surface area may be measured through the BELSORP-mini II (BEL Japan, Inc.) equipment.
- the total pore volume may be measured from a BET plot using a BELSORP-mini II (BEL Japan, Inc.) equipment.
- a method of manufacturing a negative electrode active material according to an embodiment of the present invention includes the steps of forming composite particles by mixing a carbonaceous core and a pitch and performing a first heat treatment; And mixing the composite particles and the pitch and performing a second heat treatment.
- the step of forming the composite particles may include mixing a carbonaceous core and a pitch and performing a first heat treatment.
- the average particle diameter (D 50 ) of the carbonaceous core may be 7 ⁇ m to 25 ⁇ m, specifically 8 ⁇ m to 23 ⁇ m, and more specifically 14 ⁇ m to 22 ⁇ m. If the above range is satisfied, particle agglomeration during pitch coating can be minimized.
- the carbonaceous core may include at least one selected from the group consisting of natural graphite, artificial graphite, and mesocarbone microbeads (MCMB).
- MCMB mesocarbone microbeads
- the carbonaceous core may include a carbonaceous matrix and secondary particles in which a plurality of natural graphite particles are granulated with each other.
- the secondary particles may be spherical.
- the plurality of natural graphite contained in the secondary particles may be formed by modifying the scale-like natural graphite.
- the plurality of natural graphite may be formed by agglomeration of the scale-like natural graphite, and more specifically, the natural graphite may be bonded to each other by drying the scale-like natural graphite, whereby the secondary particles are spherical To a spherical shape.
- the degree of sphericity of the secondary particles may be 0.73 to 0.97, specifically 0.83 to 0.96, and more specifically 0.92 to 0.95. If the above range is satisfied, the negative electrode can be manufactured with high density, and the negative electrode adhesion (a force that prevents the negative electrode active material from being separated from the negative electrode) is improved.
- the degree of sphericity may be measured by a digital image analysis method by capturing a 2D image of 3D particles (for example, using the equipment name Morphologi4 (Malvern)).
- the carbonaceous matrix may serve to maintain a state in which the plurality of natural graphites are bonded.
- the carbonaceous matrix may include amorphous carbon.
- the method of manufacturing a negative active material of the present invention may further include preparing a carbonaceous core.
- Preparing the carbonaceous core may include mixing a plurality of scale-like natural graphite and pitch and then sphericalizing, and thus, the carbonaceous core including the secondary particles may be formed.
- the spheroidization may be performed by repeatedly folding or assembling scale-like natural graphite by controlling the rotor speed or time in equipment such as milling.
- Preparing the carbonaceous core may further include removing internal pores of particles formed by mixing the plurality of scale-like natural graphite and pitch and then spheronizing.
- a method of removing the internal pores of the particles a method of filling the internal pores with a pitch, cold isostatic pressing (CIP), or the like may be performed.
- CIP cold isostatic pressing
- the pore volume of the prepared secondary particles may be at a low level.
- the specific surface area of the negative active material may be controlled through the step of controlling the internal pores, side reactions of the electrolyte solution may be reduced.
- the pitch mixed with the carbonaceous core may be any one of a petroleum pitch and a coal pitch.
- the weight ratio of the carbonaceous core and the pitch may be 1:0.010 to 1:0.056, specifically 1:0.040 to 1:0.056, and more specifically 1:0.045 To 1:0.056.
- the interfacial resistance is sufficiently low to improve the rapid charging performance of the battery, the capacity of the negative electrode active material is maintained at a high level, and the rapid increase in the specific surface area during negative electrode rolling is suppressed, resulting in initial efficiency and battery high temperature storage performance. This can be improved.
- the first heat treatment may be performed at a temperature of 1000° C. to 1400° C., specifically, may be performed at a temperature of 1050° C. to 1350° C., and more specifically, may be performed at a temperature of 1100° C. to 1300° C.
- a first carbon coating layer may be formed on the carbonaceous core.
- the weight ratio of the composite particles and the pitch may be 1:0.010 to 1:0.052, specifically 1:0.035 to 1:0.052, more specifically 1 It may be from :0.045 to 1:0.052.
- the second heat treatment may be performed at a temperature of 1000°C to 1400°C, specifically at a temperature of 1050°C to 1350°C, and more specifically at a temperature of 1100°C to 1300°C.
- a second carbon coating layer may be formed on the first carbon coating layer.
- the pores of the carbonaceous core can be sufficiently filled through two pitch mixing and heat treatment, and a carbon coating layer having a relatively smooth surface can be formed on the carbonaceous core (at a level with a low total pore volume). Applicable). Accordingly, since the contact area between the point-type binder such as SBR and the carbonaceous core can be secured, adhesion of the negative electrode can be improved.
- a negative active material according to another embodiment of the present invention includes a carbonaceous core and a carbon coating layer, and may have a total pore volume of 0.003 cm 3 /g to 0.010 cm 3 /g.
- the carbonaceous core is the same as the carbonaceous core introduced in the method of manufacturing the negative active material described above, and thus a description thereof is omitted.
- the carbon coating layer may be disposed on the carbonaceous core, and specifically, the carbon coating layer may cover at least a part of the surface of the carbonaceous core.
- the carbon coating layer includes amorphous carbon, and specifically may be made of amorphous carbon.
- the carbon coating layer may be formed through'the step of mixing the carbonaceous core and the pitch and performing a first heat treatment to form composite particles, mixing the composite particles with the pitch, and then performing a second heat treatment' introduced in the above-described embodiment. have.
- the total pore volume of the negative active material may be 0.003cm 3 /g to 0.010cm 3 /g, specifically 0.0035cm 3 /g to 0.0090cm 3 /g, specifically 0.0035cm 3 /g to 0.0045cm 3 /g may be.
- the total pore volume is less than 0.003cm 3 /g, the ion conductivity is lowered due to the limited contact area between the electrolyte and the negative electrode active material, which is disadvantageous for high rate charging and discharging of the battery.
- the pore volume of 0.003 cm 3 /g to 0.010 cm 3 /g corresponds to a numerical range derived since pores on the carbonaceous core can be effectively filled by two coatings through a pitch.
- the BET specific surface area of the negative active material may be 0.5m 2 /g to 2.0m 2 /g, specifically 1.0m 2 /g to 1.9m 2 /g, more specifically 1.0m 2 /g to 1.4 It may be m 2 /g.
- a negative electrode according to another exemplary embodiment of the present invention may include the negative electrode active material of the above-described exemplary embodiment.
- the negative electrode may include a negative active material layer, and specifically, may include a current collector and the negative active material layer.
- the current collector is not particularly limited as long as it has conductivity without causing a chemical change in the battery.
- copper, stainless steel, aluminum, nickel, titanium, calcined carbon, or a surface-treated aluminum or stainless steel surface with carbon, nickel, titanium, silver, or the like may be used.
- a transition metal that adsorbs carbon well, such as copper and nickel can be used as the current collector.
- the thickness of the current collector may be 6 ⁇ m to 20 ⁇ m, but the thickness of the current collector is not limited thereto.
- the negative active material layer may be disposed on the current collector.
- the negative active material layer may be disposed on at least one surface of the current collector, and specifically, may be disposed on one or both surfaces.
- the negative active material layer may include a negative active material, and in this case, the negative active material may be the negative active material of the above-described embodiment.
- the negative electrode may further include at least one of a binder and a conductive material.
- the binder is polyvinylidene fluoride-hexafluoropropylene copolymer (PVDF-co-HFP), polyvinylidenefluoride, polyacrylonitrile, polymethylmethacrylate, polymethylmethacrylate, and polyvinylidene fluoride.
- Vinyl alcohol carboxymethyl cellulose (CMC), starch, hydroxypropyl cellulose, regenerated cellulose, polyvinylpyrrolidone, tetrafluoroethylene, polyethylene, polypropylene, polyacrylic acid, ethylene-propylene-diene monomer (EPDM), alcohol It may include at least any one selected from the group consisting of phonated EPDM, styrene butadiene rubber (SBR), fluorine rubber, poly acrylic acid, and a material in which hydrogen thereof is substituted with Li, Na, or Ca, etc., It may also include various copolymers thereof.
- the conductive material is not particularly limited as long as it has conductivity without causing a chemical change in the battery, and examples thereof include graphite such as natural graphite or artificial graphite; Carbon blacks such as acetylene black, Ketjen black, channel black, Parnes black, lamp black, and thermal black; Conductive fibers such as carbon fibers and metal fibers; Conductive tubes such as carbon nanotubes; Metal powders such as fluorocarbon, aluminum, and nickel powder; Conductive whiskers such as zinc oxide and potassium titanate; Conductive metal oxides such as titanium oxide; Conductive materials such as polyphenylene derivatives may be used.
- graphite such as natural graphite or artificial graphite
- Carbon blacks such as acetylene black, Ketjen black, channel black, Parnes black, lamp black, and thermal black
- Conductive fibers such as carbon fibers and metal fibers
- Conductive tubes such as carbon nanotubes
- Metal powders such as fluorocarbon, aluminum, and nickel powder
- Conductive whiskers such
- a secondary battery according to another embodiment of the present invention may include a negative electrode, and the negative electrode is the same as the negative electrode of the above-described embodiment.
- the secondary battery may include the negative electrode, the positive electrode, a separator interposed between the positive electrode and the negative electrode, and an electrolyte, and the negative electrode is the same as the negative electrode described above. Since the cathode has been described above, a detailed description will be omitted.
- the positive electrode may include a positive electrode current collector and a positive electrode active material layer formed on the positive electrode current collector and including the positive electrode active material.
- the positive electrode current collector is not particularly limited as long as it has conductivity without causing chemical changes to the battery, for example, stainless steel, aluminum, nickel, titanium, calcined carbon, or carbon on the surface of aluminum or stainless steel. , Nickel, titanium, silver, or the like may be used.
- the positive electrode current collector may generally have a thickness of 3 ⁇ m to 500 ⁇ m, and fine unevenness may be formed on the surface of the current collector to increase the adhesion of the positive electrode active material.
- it can be used in various forms such as films, sheets, foils, nets, porous bodies, foams, and nonwoven fabrics.
- the positive active material may be a commonly used positive active material.
- the positive electrode active material may include a layered compound such as lithium cobalt oxide (LiCoO 2 ) or lithium nickel oxide (LiNiO 2 ), or a compound substituted with one or more transition metals; Lithium iron oxides such as LiFe 3 O 4; Lithium manganese oxides such as formula Li 1+c1 Mn 2-c1 O 4 (0 ⁇ c1 ⁇ 0.33), LiMnO 3 , LiMn 2 O 3 , and LiMnO 2; Lithium copper oxide (Li 2 CuO 2 ); Vanadium oxides such as LiV 3 O 8 , V 2 O 5 , and Cu 2 V 2 O 7; Formula LiNi 1-c2 M c2 O 2 (here, M is at least one selected from the group consisting of Co, Mn, Al, Cu, Fe, Mg, B, and Ga, and satisfies 0.01 ⁇ c2 ⁇ 0.3) Ni-site type lithium nickel oxide; Formula LiMn
- the positive electrode active material layer may include a positive electrode conductive material and a positive electrode binder in addition to the positive electrode active material described above.
- the positive electrode conductive material is used to impart conductivity to the electrode, and in the configured battery, as long as it does not cause chemical changes and has electronic conductivity, it can be used without particular limitation.
- Specific examples include graphite such as natural graphite and artificial graphite; Carbon-based materials such as carbon black, acetylene black, ketjen black, channel black, furnace black, lamp black, thermal black, and carbon fiber; Metal powders or metal fibers such as copper, nickel, aluminum, and silver; Conductive whiskey such as zinc oxide and potassium titanate; Conductive metal oxides such as titanium oxide;
- a conductive polymer such as a polyphenylene derivative may be used, and one of them alone or a mixture of two or more may be used.
- the positive electrode binder serves to improve adhesion between positive electrode active material particles and adhesion between the positive electrode active material and the positive electrode current collector.
- specific examples include polyvinylidene fluoride (PVDF), vinylidene fluoride-hexafluoropropylene copolymer (PVDF-co-HFP), polyvinyl alcohol, polyacrylonitrile, carboxymethylcellulose (CMC).
- a separator As a separator, it separates the negative electrode and the positive electrode and provides a passage for lithium ions. If it is used as a separator in a general secondary battery, it can be used without special restrictions. It is desirable. Specifically, a porous polymer film, for example, a porous polymer film made of polyolefin-based polymers such as ethylene homopolymer, propylene homopolymer, ethylene/butene copolymer, ethylene/hexene copolymer, and ethylene/methacrylate copolymer, or these A stacked structure of two or more layers of may be used.
- polyolefin-based polymers such as ethylene homopolymer, propylene homopolymer, ethylene/butene copolymer, ethylene/hexene copolymer, and ethylene/methacrylate copolymer, or these A stacked structure of two or more layers of may be used.
- a conventional porous nonwoven fabric for example, a nonwoven fabric made of a high melting point glass fiber, polyethylene terephthalate fiber, or the like may be used.
- a coated separator containing a ceramic component or a polymer material may be used, and optionally, a single layer or a multilayer structure may be used.
- the electrolyte may include, but is not limited to, an organic liquid electrolyte, an inorganic liquid electrolyte, a solid polymer electrolyte, a gel polymer electrolyte, a solid inorganic electrolyte, and a molten inorganic electrolyte that can be used when manufacturing a lithium secondary battery.
- the electrolyte may include a non-aqueous organic solvent and a metal salt.
- non-aqueous organic solvent for example, N-methyl-2-pyrrolidinone, propylene carbonate, ethylene carbonate, butylene carbonate, dimethyl carbonate, diethyl carbonate, gamma-butyllolactone, 1,2-dime Oxyethane, tetrahydroxy franc (franc), 2-methyl tetrahydrofuran, dimethyl sulfoxide, 1,3-dioxolone, formamide, dimethylformamide, dioxolone, acetonitrile, nitromethane, methyl formate, Methyl acetate, phosphoric acid tryester, trimethoxy methane, dioxolone derivative, sulfolane, methyl sulfolane, 1,3-dimethyl-2-imidazolidinone, propylene carbonate derivative, tetrahydrofuran derivative, ether, pyrofion
- An aprotic organic solvent such as methyl acid or ethy
- ethylene carbonate and propylene carbonate which are cyclic carbonates
- the metal salt may be a lithium salt
- the lithium salt is a material that is readily soluble in the non-aqueous electrolyte, for example, is in the lithium salt anion F -, Cl -, I - , NO 3 -, N (CN ) 2 -, BF 4 -, ClO 4 -, PF 6 -, (CF 3) 2 PF 4 -, (CF 3) 3 PF 3 -, (CF 3) 4 PF 2 -, (CF 3) 5 PF - , (CF 3) 6 P - , CF 3 SO 3 -, CF 3 CF 2 SO 3 -, (CF 3 SO 2) 2 N -, (FSO 2) 2 N -, CF 3 CF 2 (CF 3) 2 CO -, (CF 3 SO 2 ) 2 CH -, (SF 5) 3 C -, (CF 3 SO 2) 3 C -, CF 3 (CF 2) 7 SO 3 -, CF 3 CO 2 -, CH 3 CO 2 -
- the electrolyte includes, for example, haloalkylene carbonate-based compounds such as difluoroethylene carbonate, pyridine, and trivalent for the purpose of improving the life characteristics of the battery, suppressing the reduction in battery capacity, and improving the discharge capacity of the battery.
- haloalkylene carbonate-based compounds such as difluoroethylene carbonate, pyridine, and trivalent for the purpose of improving the life characteristics of the battery, suppressing the reduction in battery capacity, and improving the discharge capacity of the battery.
- Ethyl phosphite triethanolamine, cyclic ether, ethylene diamine, n-glyme, hexaphosphate triamide, nitrobenzene derivative, sulfur, quinone imine dye, N-substituted oxazolidinone, N,N-substituted imida
- One or more additives such as zolidine, ethylene glycol dialkyl ether, ammonium salt, pyrrole, 2-methoxy ethanol, or aluminum trichloride may be further included.
- a battery module including the secondary battery as a unit cell and a battery pack including the same are provided. Since the battery module and the battery pack include the secondary battery having high capacity, high rate characteristics, and site characteristics, a mid- to large-sized device selected from the group consisting of electric vehicles, hybrid electric vehicles, plug-in hybrid electric vehicles, and power storage systems It can be used as a power source.
- the carbonaceous core and pitch were mixed in a weight ratio of 1:0.049, and then stirred with a mixer. Thereafter, the mixture was heat-treated at 1200° C. for 8 hours to prepare composite particles.
- the composite particles and pitch were mixed in a weight ratio of 1:0.047, and then stirred with a mixer. Thereafter, the mixture was heat-treated at 1300° C. for 9 hours to prepare a negative active material.
- the carbonaceous core and pitch were mixed in a weight ratio of 1:0.043, and then stirred with a mixer. Thereafter, the mixture was heat-treated at 1250° C. for 7 hours to prepare composite particles.
- the composite particles and pitch were mixed in a weight ratio of 1:0.042, and then stirred with a mixer. Thereafter, the mixture was heat-treated at 1300° C. for 9 hours to prepare a negative active material.
- the mixture was stirred with a mixer. Thereafter, the mixture was heat-treated at 1200° C. for 7 hours to prepare composite particles.
- the composite particles and pitch were mixed in a weight ratio of 1:0.031, and then stirred with a mixer. Thereafter, the mixture was heat-treated at 1300° C. for 9 hours to prepare a negative active material.
- the carbonaceous core and pitch were mixed in a weight ratio of 1:0.043, and then stirred with a mixer. Thereafter, the mixture was heat-treated at 1300° C. for 6 hours to prepare composite particles.
- the composite particles and pitch were mixed in a weight ratio of 1:0.042, and then stirred with a mixer. Thereafter, the mixture was heat-treated at 1300° C. for 8 hours to prepare a negative active material.
- Example 1 The carbonaceous core and pitch used in Example 1 were mixed in a weight ratio of 1:0.064, and then stirred with a mixer. Thereafter, the mixture was heat-treated at 1300° C. for 10 hours to prepare composite particles.
- the BET specific surface area was measured using a BELSORP-mini II (BEL Japan, Inc.) equipment.
- the total pore volume was measured from a BET plot using a BELSORP-mini II (BEL Japan, Inc.) equipment.
- a negative electrode was manufactured in the following manner.
- each negative active material, Super C65 as a conductive material, styrene butadiene rubber (SBR) as a binder, and carboxymethylcellulose (CMC) as a thickener were mixed in a weight ratio of 96.6:1:1.3:1.1, respectively, and water Added to prepare a negative electrode slurry.
- the negative electrode slurry was applied to a copper foil (current collector) and then vacuum-dried at 130° C. for 10 hours to prepare a negative electrode (1.4875 cm 2 ).
- the loading amount of the prepared negative electrode was 3.61mAh/cm 2 .
- the negative electrode was punched out at 20 mm ⁇ 150 mm and fixed to the center of the 25 mm ⁇ 75 mm slide glass using a tape, and then peeling off the current collector using UTM, and peeling strength was measured at 90 degrees. In the evaluation, five or more peeling strengths were measured and set as an average value, which is shown in Table 2.
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Abstract
Description
| 음극 활물질의 BET비표면적(m2/g) | 총 기공 부피(10-3cm3/g) | |
| 실시예 1 | 1.2 | 3.9 |
| 실시예 2 | 1.6 | 5.0 |
| 실시예 3 | 1.4 | 4.2 |
| 실시예 4 | 1.9 | 8.9 |
| 비교예 1 | 2.8 | 16.7 |
| 음극 접착력(gf/10mm) | |
| 실시예 1 | 30 |
| 실시예 2 | 27 |
| 실시예 3 | 25 |
| 실시예 4 | 18 |
| 비교예 1 | 14 |
Claims (15)
- 탄소질 코어 및 피치를 혼합하고 제1 열처리하여 복합 입자를 형성하는 단계; 및상기 복합 입자와 피치를 혼합하고 제2 열처리하는 단계;를 포함하는 음극 활물질의 제조 방법.
- 청구항 1에 있어서,상기 제1 열처리는 1000℃ 내지 1400℃의 온도에서 수행되는 음극 활물질의 제조 방법.
- 청구항 1에 있어서,상기 제2 열처리는 1000℃ 내지 1400℃의 온도에서 수행되는 음극 활물질의 제조 방법.
- 청구항 1에 있어서,상기 복합 입자를 형성하는 단계에 있어서,상기 탄소질 코어와 상기 피치의 중량비는 1:0.010 내지 1:0.056인 음극 활물질의 제조 방법.
- 청구항 1에 있어서,상기 복합 입자와 피치를 혼합하고 제2 열처리하는 단계에 있어서,상기 복합 입자와 상기 피치의 중량비는 1:0.010 내지 1:0.052인 음극 활물질의 제조 방법.
- 청구항 1에 있어서,상기 탄소질 코어의 평균 입경(D50)은 7㎛ 내지 25㎛인 음극 활물질의 제조 방법.
- 청구항 1에 있어서,상기 탄소질 코어는 천연흑연, 인조흑연, 및 MCMB로 이루어진 군에서 선택되는 적어도 어느 하나를 포함하는 음극 활물질의 제조 방법.
- 청구항 1에 있어서,상기 탄소질 코어는 탄소질 매트릭스 및 복수의 천연흑연 입자가 서로 조립화된 2차 입자를 포함하는 음극 활물질의 제조 방법.
- 청구항 1에 있어서,상기 탄소질 코어를 준비하는 단계를 더 포함하며,상기 탄소질 코어를 준비하는 단계는,복수의 인편상 천연흑연 및 피치를 혼합한 뒤 구형화하는 것을 포함하는 음극 활물질의 제조 방법.
- 청구항 9에 있어서,상기 구형화 이후 내부 기공을 제거하는 단계를 더 포함하는 음극 활물질의 제조 방법.
- 탄소질 코어 및 탄소 코팅층을 포함하며,총 기공 부피가 0.003cm3/g 내지 0.010cm3/g인 음극 활물질.
- 청구항 11에 있어서,BET비표면적이 0.5m2/g 내지 2.0m2/g인 음극 활물질.
- 청구항 11에 있어서,상기 탄소질 코어의 평균 입경(D50)은 7㎛ 내지 25㎛인 음극 활물질.
- 청구항 11의 음극 활물질을 포함하는 음극.
- 청구항 14의 음극을 포함하는 이차 전지.
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| CN202080071962.XA CN114556625B (zh) | 2019-10-28 | 2020-10-23 | 制备负极活性材料的方法、负极活性材料、包含其的负极以及包括所述负极的二次电池 |
| US17/768,683 US20240034632A1 (en) | 2019-10-28 | 2020-10-23 | Method for producing negative electrode active material, negative electrode active material, negative electrode including the same, and secondary battery including the negative electrode |
| EP20883560.3A EP4030506A4 (en) | 2019-10-28 | 2020-10-23 | PROCESS FOR MANUFACTURE OF ANODE ACTIVE MATERIAL, ANODE ACTIVE MATERIAL, ANODE THEREOF AND SECONDARY BATTERY WITH THIS ANODE |
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| USD1047997S1 (en) | 2022-12-06 | 2024-10-22 | Samsung Electronics Co., Ltd. | Notebook computer |
| KR102831511B1 (ko) * | 2023-01-20 | 2025-07-08 | (주)포스코퓨처엠 | 리튬 이차 전지용 음극 및 이를 포함하는 리튬 이차 전지 |
| KR102711530B1 (ko) * | 2023-09-14 | 2024-09-27 | 윤성영 | 다층 탄소 복합체의 제조방법 |
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-
2019
- 2019-10-28 KR KR1020190134845A patent/KR102789807B1/ko active Active
-
2020
- 2020-10-23 EP EP20883560.3A patent/EP4030506A4/en active Pending
- 2020-10-23 CN CN202080071962.XA patent/CN114556625B/zh active Active
- 2020-10-23 WO PCT/KR2020/014567 patent/WO2021085946A1/ko not_active Ceased
- 2020-10-23 US US17/768,683 patent/US20240034632A1/en active Pending
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| EP4030506A4 (en) | 2022-12-21 |
| KR20210050348A (ko) | 2021-05-07 |
| EP4030506A1 (en) | 2022-07-20 |
| KR102789807B1 (ko) | 2025-04-03 |
| CN114556625A (zh) | 2022-05-27 |
| US20240034632A1 (en) | 2024-02-01 |
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