CN106328935A - High-safety long-life composite material system power battery and preparation method thereof - Google Patents

High-safety long-life composite material system power battery and preparation method thereof Download PDF

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CN106328935A
CN106328935A CN201610780828.2A CN201610780828A CN106328935A CN 106328935 A CN106328935 A CN 106328935A CN 201610780828 A CN201610780828 A CN 201610780828A CN 106328935 A CN106328935 A CN 106328935A
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battery
life
electrokinetic cell
composite system
safety long
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王光俊
吴小兰
陈炜
张宏立
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Gotion High Tech Co Ltd
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Gotion High Tech Co Ltd
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/52Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
    • H01M4/525Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/4235Safety or regulating additives or arrangements in electrodes, separators or electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/50Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
    • H01M4/505Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/60Selection of substances as active materials, active masses, active liquids of organic compounds
    • H01M4/602Polymers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624Electric conductive fillers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624Electric conductive fillers
    • H01M4/625Carbon or graphite
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2220/00Batteries for particular applications
    • H01M2220/20Batteries in motive systems, e.g. vehicle, ship, plane
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Secondary Cells (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

The invention relates to the field of research and development and preparation of lithium batteries, in particular to a composite material system power battery with high safety and long service life and a preparation method thereof. The manufacturing method of the power battery comprises the following steps: mixing 70-90% of nickel cobalt lithium manganate and 10-30% of lithium manganese phosphate, fully mixing with a high-conductivity carbon nano tube, then, rolling and slitting a coating to prepare a positive plate, fully mixing a negative electrode with artificial graphite and acetylene black, then, rolling and slitting to prepare a negative plate, preparing a battery core by a diaphragm by adopting a wet polyethylene substrate, an aluminum oxide ceramic coating and a binder PVDF according to a required size, and then, injecting liquid to form a partial volume to prepare the battery, wherein the electrolyte is a high-molar-concentration mixed solvent system of various composite additives. The prepared battery has a retention rate of 88 percent after being cycled at normal temperature for 1200 weeks and a retention rate of 87 percent after being cycled at high temperature of 45 ℃ for 680 weeks, has good thermal stability, energy density, normal temperature and high temperature cycle performance and excellent safety, and can be widely applied to electric automobiles and related products.

Description

A kind of composite system electrokinetic cell of high-safety long-life and preparation method thereof
Technical field
The present invention relates to the research and development preparation field of lithium battery, be specifically related to the composite system of a kind of high-safety long-life Electrokinetic cell and preparation method thereof.
Background technology
Reach under the target of 300Wh/kg orders about in the energy density of the year two thousand twenty battery module to be realized, nickelic ternary material Become the focus of research and development, but domestic nickelic ternary battery in use safety be without shortcomings such as guarantee, high temperature cyclic performance differences, At the beginning of 2016, Ministry of Industry and Information promulgate postpone in commercial car use ternary material power lithium-ion battery, cause ternary lithium from Sub-battery enterprise in commotion, my department, as power lithium-ion battery leading enterprise, takes the lead in strengthening ternary lithium ion battery The R&D intensity of security performance.Patent CN104300123A uses the method that nickel-cobalt-manganese ternary material is mixed with iron manganese phosphate for lithium, The method is given prominence to the key points being mixed into of iron manganese phosphate for lithium, ternary battery safety nickelic to all types and the shadow of cycle performance Ringing, the present invention is then just for high-nickel material LiNi0.6Co0.2Mn0.2O2With LiMn0.8Fe0.2PO4Many-sided both different blended of investigation Composition and division in a proportion example and the combination of the auxiliary material impact on battery combination property, provides more safe and reliable foundation for reality application.
Summary of the invention
Present invention aim to address above-mentioned the deficiencies in the prior art, improve high-nickel material LiNi0.6Co0.2Mn0.2O2Combine Close performance, it is provided that composite system electrokinetic cell of a kind of high-safety long-life and preparation method thereof.
The present invention is achieved by the following technical solutions:
The composite system electrokinetic cell of a kind of high-safety long-life, including positive pole, barrier film, negative pole, electrolyte and outer Shell, described
Positive pole includes the component of following mass percent: 93~the polyethylene pyrrole of the positive active material of 97%, 1~2% Pyrrolidone (PVP), 1~3.5% CNT (CNTs) and 1~the Kynoar (PVDF) of 3.5%;Slurry viscosity: 6000 ~9000mPa.S;
Wherein, positive active material is high-nickel material LiNi0.6Co0.2Mn0.2O2And LiMn (NCM)0.8Fe0.2PO4 (LMFP) Mixture, and LiNi0.6Co0.2Mn0.2O2Account for the 70~90% of positive active material gross mass, LiMn0.8Fe0.2PO4Account for positive pole The 10~30% of active substance gross mass;
Negative pole includes the component of following mass percent: 93~the graphite of 96%, 1~the acetylene black of 3%, 1~the carboxylic of 3% Sodium carboxymethylcellulose pyce and 1.5~the butadiene-styrene rubber of 3%;Slurry viscosity: 3000~5000mPa S;
Barrier film is coated separator, and described diaphragm matrix is wet method polyethylene (PE), and coating is pottery (Al2O3Or SiO2), viscous Knot agent is Kynoar-hexafluoropropene (PVDF-HFP), Kynoar (PVDF) or polymethyl methacrylate (PMMA), Barrier film gross thickness is 12~20 μm;
Electrolyte includes the electrolyte LiPF that concentration is 0.9mol/L~1.2mol/L6, vinyl carbonate (EC), carbonic acid first Ethyl ester (EMC) and dimethyl carbonate (DMC) press the organic solvent of the volume ratio mixing of 1:1:1, and include 1~2% carbonic acid sub- Vinyl acetate (VC), 1~2% propylene sulfite (PS), 0~1% biphenyl (BP) and 0~1% cyclohexyl benzene (CHB) add at interior Add agent.
Preferably, the aluminium foil that described positive pole uses collector thickness to be 12~18 μm.
Preferably, the Copper Foil that described negative pole uses collector thickness to be 8~12 μm.
Preferably, described anode pole piece applies 1~5mm ceramic sol with lug adjoining border, and ceramic sol is by Al2O3With N-Methyl pyrrolidone (NMP) forms, and Al2O3Account for the 15~30% of ceramic sol gross mass.
Preferably, the caliber of described CNT is 10~30nm.
Preferably, described positive pole double-coated surface density is 340~430kg/m2, negative pole double-coated surface density is 190 ~240kg/m2
Preferably, described shell is aluminum hull, box hat or moulds shell.
The method preparing the composite system electrokinetic cell of a kind of high-safety long-life, comprises the following steps:
(1), with NMP as solvent, after being completely dissolved PVDF (molecular weight 90~1,000,000), CNTs high speed dispersion is added, then It is mixed into LiNi0.6Co0.2Mn0.2O2And LiMn0.8Fe0.2PO4Positive active material, uses coating machine even application to exist after fully closing slurry On aluminium foil, drying, roll-in, cut after, make anode pole piece;
(2), with deionized water as solvent, after being completely dispersed dissolving sodium carboxymethyl cellulose, it is mixed into conductive agent acetylene black and bears Pole active substance Delanium, the most again with binding agent butadiene-styrene rubber mixed pulp, is then coated on Copper Foil, baking, roll-in, Cathode pole piece is made after cutting;
(3) according to required positive/negative plate size, use coated separator, be wound into battery core, then two battery cores link shell Rear Laser Welding, fluid injection, chemical conversion, make battery.
The beneficial effects of the present invention is:
In the present invention, the aluminum-shell battery of making uses anode composite system, improves the general safety stability of battery system. Lithium ion battery running voltage is 3.0~4.2V, uses this scope running voltage, can substantially reduce the electricity that high voltage system is brought Solve matter resolution problem, and then battery table reveals good cycle performance;Anode pole piece and lug adjoining border coating 1~5mm pottery Porcelain cement body, on the one hand can improve pole piece and cut the burr being occur, on the other hand can improve the heat stability of battery;Positive conductive Agent CNT, fluid behaviour can limited improvement stir uneven, and CNT also has the highest electric conductivity simultaneously;Electrolysis In liquid, the addition of additive can be obviously improved security performance and the cycle performance of battery, particularly high temperature cyclic performance.The present invention Making battery room temperature 1200 weeks conservation rates 88% of circulation, high temperature 45 DEG C circulates 680 weeks conservation rates 87%, has good thermally-stabilised Property, energy density, room temperature, high temperature cyclic performance and excellent safety, can be widely used for electric automobile and Related product.
Accompanying drawing explanation
Fig. 1 is LiNi of the present invention0.6Co0.2Mn0.2O2:LiMn0.8Fe0.2PO4Composite scanning electron microscope (SEM) photograph during=8:2;
Fig. 2 is the room temperature circulation figure of the battery that the embodiment of the present invention is prepared with comparative example;
Fig. 3 is the high temperature circulation figure of the battery that the embodiment of the present invention is prepared with comparative example;
Fig. 4 is acupuncture effect figure of the present invention;
Fig. 5 is that in acupuncture course of the present invention, voltage changes over curve.
Detailed description of the invention
For being best understood from the present invention, below in conjunction with embodiment and accompanying drawing, the invention will be further described, following example It is only that the present invention will be described rather than is limited it.
Embodiment one
The present embodiment use coated separator use 14 μm PE to be base material, 4 μm Al2O3Coating (i.e. 14+4).
1), with NMP as solvent, after being completely dissolved PVDF, add CNT high speed dispersion, be then mixed into anode composite and live Property material (LiNi0.6Co0.2Mn0.2O2:LiMn0.8Fe0.2PO4=8:2), use coating machine even application at aluminium foil after fully closing slurry On, drying, roll-in, cut after, make anode pole piece, PVP 1~2%, PVDF 1~3.5%, CNT 1~3.5%, slurry Material viscosity: 6000~9000mPa.S, positive pole applicator surface density 370kg/m2, slurry edge coating 2mm Al2O3Ceramic sol.Negative Pole is with deionized water as solvent, after being completely dispersed CMC, is mixed into acetylene black and negative electrode active material Delanium, the most again with SBR Mixed pulp, is then coated on Copper Foil, baking, roll-in, cut after make cathode pole piece.Mixed proportion: graphite 93~ 96%, acetylene black 1~3%, sodium carboxymethyl cellulose 1~3%, butadiene-styrene rubber 1.5~3.5%.Slurry viscosity: 3000~ 5000mPa S, negative pole applicator surface density 205kg/m2
2), according to required positive/negative plate size, use 14+4 coated separator, be wound into battery core, then two battery core parallel connections Enter Laser Welding after shell, inject containing 1.1mol/L LiPF6/ (EC+EMC+DMC, volume ratio 1:1:1), 2%VC, 2%PS, 1% The electrolyte of BP, is melted into, makes battery.
Embodiment two
The present embodiment use coated separator use 12 μm PE to be base material, 4 μm Al2O3With 2 μm PVDF coating (i.e. 12+4 +2)。
1), with NMP as solvent, after being completely dissolved PVDF, add CNT high speed dispersion, be then mixed into anode composite and live Property material (LiNi0.6Co0.2Mn0.2O2:LiMn0.8Fe0.2PO4=8:2), use coating machine even application at aluminium foil after fully closing slurry On, drying, roll-in, cut after, make anode pole piece, PVP 1~2%, PVDF 1~3.5%, CNT 1~3.5%, slurry Material viscosity: 6000~9000mPa.S, positive pole applicator surface density 370kg/m2, slurry edge coating 2mm Al2O3Ceramic sol.Negative Pole is with deionized water as solvent, after being completely dispersed CMC, is mixed into acetylene black and negative electrode active material Delanium, the most again with SBR Mixed pulp, is then coated on Copper Foil, baking, roll-in, cut after make cathode pole piece.Mixed proportion: graphite 93~96%, Acetylene black 1~3%, sodium carboxymethyl cellulose 1~3%, butadiene-styrene rubber 1.5~3.5%.Slurry viscosity: 3000~5000mPa S, negative pole applicator surface density 205kg/m2
2), according to required positive/negative plate size, using 12+4+2 coated separator, be wound into battery core, then two battery cores are also Link Laser Welding after shell, inject containing 1.1mol/L LiPF6/ (EC+EMC+DMC, volume ratio 1:1:1), 2%VC, 2%PS, The electrolyte of 1%BP, is melted into, makes battery.
Embodiment three
The present embodiment use coated separator use 12 μm PE to be base material, 4 μm Al2O31 μm PVDF coating each with two sides (i.e. 12+4+1+1).
1), with NMP as solvent, after being completely dissolved PVDF, add CNT high speed dispersion, be then mixed into anode composite and live Property material (LiNi0.6Co0.2Mn0.2O2:LiMn0.8Fe0.2PO4=8:2), use coating machine even application at aluminium foil after fully closing slurry On, drying, roll-in, cut after, make anode pole piece, PVP 1~2%, PVDF 1~3.5%, CNT 1~3.5%, slurry Material viscosity: 6000~9000mPa.S, positive pole applicator surface density 370kg/m2, slurry edge coating 2mm Al2O3Ceramic sol.Negative Pole is with deionized water as solvent, after being completely dispersed CMC, is mixed into acetylene black and negative electrode active material Delanium, the most again with SBR mixed pulp, is then coated on Copper Foil, baking, roll-in, cut after make cathode pole piece.Mixed proportion: graphite 93~ 96%, acetylene black 1~3%, sodium carboxymethyl cellulose 1~3%, butadiene-styrene rubber 1.5~3.5%.Slurry viscosity: 3000~ 5000mPa S, negative pole applicator surface density 205kg/m2
2), according to required positive/negative plate size, use 12+4+1+1 coated separator, be wound into battery core, then two battery cores And link Laser Welding after shell, inject containing 1.1mol/L LiPF6/ (EC+EMC+DMC, volume ratio 1:1:1), 2%VC, 2%PS, The electrolyte of 1%BP, is melted into, makes battery.
Embodiment four
The present embodiment use coated separator use 14 μm PE to be base material, each 2 μm PVDF coatings of one side (i.e. 14+2+2).
1), with NMP as solvent, after being completely dissolved PVDF, add CNT high speed dispersion, be then mixed into anode composite and live Property material (LiNi0.6Co0.2Mn0.2O2:LiMn0.8Fe0.2PO4=8:2), use coating machine even application at aluminium foil after fully closing slurry On, drying, roll-in, cut after, make anode pole piece, PVP 1~2%, PVDF 1~3.5%, CNT 1~3.5%, slurry Material viscosity: 6000~9000mPa.S, positive pole applicator surface density 370kg/m2, slurry edge coating 2mm Al2O3Ceramic sol.Negative Pole is with deionized water as solvent, after being completely dispersed CMC, is mixed into acetylene black and negative electrode active material Delanium, the most again with SBR Mixed pulp, is then coated on Copper Foil, baking, roll-in, cut after make cathode pole piece.Mixed proportion: graphite 93~96%, Acetylene black 1~3%, sodium carboxymethyl cellulose 1~3%, butadiene-styrene rubber 1.5~3.5%.Slurry viscosity: 3000~5000mPa S, negative pole applicator surface density 205kg/m2
2), according to required positive/negative plate size, using 14+2+2 coated separator, be wound into battery core, then two battery cores are also Link Laser Welding after shell, inject containing 1.1mol/L LiPF6/ (EC+EMC+DMC, volume ratio 1:1:1), 2%VC, 2%PS, The electrolyte of 1%BP, is melted into, makes battery.
Embodiment five
The present embodiment use coated separator use 10 μm PE to be base material, each 1 μm PVDF-HFP coating (the i.e. 12+4 of one side +1+1)。
1), with NMP as solvent, after being completely dissolved PVDF, add CNT high speed dispersion, be then mixed into anode composite and live Property material (LiNi0.6Co0.2Mn0.2O2:LiMn0.8Fe0.2PO4=9:1), use coating machine even application at aluminium foil after fully closing slurry On, drying, roll-in, cut after, make anode pole piece, PVP 1~2%, PVDF 1~3.5%, CNT 1~3.5%, slurry Material viscosity: 6000~9000mPa.S, positive pole applicator surface density 340kg/m2, slurry edge coating 2mm Al2O3Ceramic sol. Negative pole is with deionized water as solvent, after being completely dispersed CMC, is mixed into acetylene black and negative electrode active material Delanium, the most again with SBR mixed pulp, is then coated on Copper Foil, baking, roll-in, cut after make cathode pole piece.Mixed proportion: graphite 93~ 96%, acetylene black 1~3%, sodium carboxymethyl cellulose 1~3%, butadiene-styrene rubber 1.5~3.5%.Slurry viscosity: 3000~ 5000mPa S, negative pole applicator surface density 190kg/m2
2), according to required positive/negative plate size, using 10+1+1 coated separator, be wound into battery core, then two battery cores are also Link Laser Welding after shell, inject containing 0.9mol/L LiPF6/ (EC+EMC+DMC, volume ratio 1:1:1), 1%VC, 1%PS, The electrolyte of 1%CHB, is melted into, makes battery.
Embodiment six
The present embodiment use coated separator use 12 μm PE to be base material, 4 μm SiO22 μm PMMA coatings each with two sides are (i.e. 12+4+1+1)。
1), with NMP as solvent, after being completely dissolved PVDF, add CNT high speed dispersion, be then mixed into anode composite and live Property material (LiNi0.6Co0.2Mn0.2O2:LiMn0.8Fe0.2PO4=7:3), use coating machine even application at aluminium foil after fully closing slurry On, drying, roll-in, cut after, make anode pole piece, PVP 1~2%, PVDF 1~3.5%, CNT 1~3.5%, slurry Material viscosity: 6000~9000mPa.S, positive pole applicator surface density 430kg/m2, slurry edge coating 2mm Al2O3Ceramic sol.Negative Pole is with deionized water as solvent, after being completely dispersed CMC, is mixed into acetylene black and negative electrode active material Delanium, the most again with SBR Mixed pulp, is then coated on Copper Foil, baking, roll-in, cut after make cathode pole piece.Mixed proportion: graphite 93~96%, Acetylene black 1~3%, sodium carboxymethyl cellulose 1~3%, butadiene-styrene rubber 1.5~3.5%.Slurry viscosity: 3000~5000mPa S, negative pole applicator surface density 240kg/m2
2), according to required positive/negative plate size, use 12+4+2+2 coated separator, be wound into battery core, then two battery cores And link Laser Welding after shell, inject containing 1.2mol/L LiPF6/ (EC+EMC+DMC, volume ratio 1:1:1), 2%VC, 2%PS, The electrolyte of 1%BP, 1%CHB, is melted into, makes battery.
Comparative example
The present embodiment use coated separator use 14 μm PE to be base material, 4 μm Al2O3Coating (i.e. 14+4).
1), with NMP as solvent, after being completely dissolved PVDF, add CNT high speed dispersion, be then mixed into positive electrode active material Matter (LiNi0.6Co0.2Mn0.2O2), use after fully closing slurry coating machine even application on aluminium foil, dryings, roll-in, cut after, make Become anode pole piece, PVP 1~2%, PVDF 1~3.5%, CNT 1~3.5%, slurry viscosity: 6000~ 9000mPa.S, positive pole applicator surface density 370kg/m2.Negative pole is with deionized water as solvent, after being completely dispersed CMC, is mixed into acetylene Black and negative electrode active material Delanium, the most again with SBR mixed pulp, is then coated on Copper Foil, baking, roll-in, cuts After make cathode pole piece.Mixed proportion: graphite 93~96%, acetylene black 1~3%, sodium carboxymethyl cellulose 1~3%, butylbenzene rubber Glue 1.5~3.5%.Slurry viscosity: 3000~5000mPa S, negative pole applicator surface density 205kg/m2
2), according to required positive/negative plate size, use 14+4 coated separator, be wound into battery core, then two battery core parallel connections Enter Laser Welding after shell, inject containing 1.1mol/L LiPF6/ (EC+EMC+DMC, volume ratio 1:1:1), 2%VC, 2%PS, 1% The electrolyte of BP, is melted into, makes battery.
1), lithium ion battery uses takeup type structure in experimental example, is fabricated to the square aluminum housing battery of 27Ah.
2), experimental example makes constant voltage to electric current after the circulation of battery room temperature uses 1C to charge to 4.2V and reaches 0.05C eventually Only, static 1h, constant-current discharge to 3.0V.
3) experimental example makes battery high-temperature cycle battery and be incubated after 5h, 1C charge to 4.2V constant voltage extremely at calorstat Electric current reaches 0.05C and terminates, static 1h, constant-current discharge to 3.0V.
4) in experimental example, safety experiment all uses GB/T 31485-2015 " power accumulator safety requirements used for electric vehicle And test method "
5) acupuncture experiment test effect is shown in that Fig. 4, Fig. 5 are that in acupuncture course, voltage changes over curve, it can be seen that real Test in example that battery is after acupuncture, apparent unchanged, the most on fire do not explode, cell voltage slowly declines and thermal runaway does not occur.
Fig. 1 is experimental example one to four, LiNi0.6Co0.2Mn0.2O2And LiMn0.8Fe0.2PO4Compound proportioning is positive pole during 8:2 Scanning electron microscopic picture, it can be seen that the granule dispersion of composite positive pole is very good, and electrode stability is well ensured, It is of value to room temperature and high temperature circulation.
Table 1 is the performance test results
Comparative example finds with embodiment comparing result, and such as Fig. 2-3 and table 1, lithium ferric manganese phosphate adds membership and somewhat sacrifices electricity The room temperature in pond and high temperature cyclic performance, but security performance (acupuncture, overcharge) has and clearly improves.Use the auxiliary material of barrier film with compound Positive electrode is combined, and the acupuncture of battery, overcharges almost all and is tested by GB.
The above embodiment is only to be described the preferred embodiment of the present invention, the not model to the present invention Enclose and be defined, on the premise of designing spirit without departing from the present invention, the those of ordinary skill in the art technical side to the present invention Various deformation that case is made and improvement, all should fall in the protection domain that claims of the present invention determines.

Claims (8)

1. a composite system electrokinetic cell for high-safety long-life, including positive pole, barrier film, negative pole, electrolyte and shell, It is characterized in that: described
Positive pole includes the component of following mass percent: 93~the polyvinylpyrrolidone of the positive active material of 97%, 1~2%, 1~3.5% CNT and 1~the Kynoar of 3.5%;Slurry viscosity: 6000~9000 mPa.S;
Wherein, positive active material is high-nickel material LiNi0.6Co0.2Mn0.2O2With LiMn0.8Fe0.2PO4Mixture, and LiNi0.6Co0.2Mn0.2O2Account for the 70~90% of positive active material gross mass, LiMn0.8Fe0.2PO4Account for the total matter of positive active material The 10~30% of amount;
Negative pole includes the component of following mass percent: 93~the graphite of 96%, 1~the acetylene black of 3%, 1~3% carboxymethyl fine Dimension element sodium and 1.5~the butadiene-styrene rubber of 3%;Slurry viscosity: 3000~5000 mPa.S;
Barrier film is coated separator, and described diaphragm matrix is wet method polyethylene, and coating is pottery, and binding agent is Kynoar-six Fluoropropene, Kynoar or polymethyl methacrylate, barrier film gross thickness is 12~20 μm;
Electrolyte includes the electrolyte LiPF that concentration is 0.9mol/L~1.2mol/L6, vinyl carbonate, Ethyl methyl carbonate and carbon Dimethyl phthalate presses the organic solvent of the volume ratio mixing of 1:1:1, and includes 1~2% vinylene carbonate, 1~2% sulfurous acid third Alkene ester, 0~1% biphenyl and 0~1% cyclohexyl benzene at interior additive.
The composite system electrokinetic cell of a kind of high-safety long-life the most according to claim 1, it is characterised in that: institute State the aluminium foil that positive pole uses collector thickness to be 12~18 μm.
The composite system electrokinetic cell of a kind of high-safety long-life the most according to claim 1, it is characterised in that: institute State the Copper Foil that negative pole uses collector thickness to be 8~12 μm.
The composite system electrokinetic cell of a kind of high-safety long-life the most according to claim 1, it is characterised in that: institute Stating anode pole piece and apply 1~5mm ceramic sol with lug adjoining border, ceramic sol is by Al2O3With N-Methyl pyrrolidone group Become, and Al2O3Account for the 15~30% of ceramic sol gross mass.
The composite system electrokinetic cell of a kind of high-safety long-life the most according to claim 1, it is characterised in that: institute The caliber stating CNT is 10~30nm.
The composite system electrokinetic cell of a kind of high-safety long-life the most according to claim 1, it is characterised in that: institute Stating positive pole double-coated surface density is 340~430 kg/m2, negative pole double-coated surface density is 190~240 kg/m2
The composite system electrokinetic cell of a kind of high-safety long-life the most according to claim 1, it is characterised in that: institute State shell to be aluminum hull, box hat or mould shell.
8. the method for the composite system electrokinetic cell of preparation high-safety long-life described in any one of claim 1-7, its It is characterised by, comprises the following steps:
(1), with N-Methyl pyrrolidone as solvent, after being completely dissolved Kynoar, CNT high speed dispersion is added, then It is mixed into LiNi0.6Co0.2Mn0.2O2And LiMn0.8Fe0.2PO4Positive active material, uses coating machine even application to exist after fully closing slurry On aluminium foil, drying, roll-in, cut after, make anode pole piece;
(2), with deionized water as solvent, after being completely dispersed dissolving sodium carboxymethyl cellulose, it is mixed into conductive agent acetylene black and negative pole is lived Property material Delanium, the most again with binding agent butadiene-styrene rubber mixed pulp, is then coated on Copper Foil, baking, roll-in, cuts After make cathode pole piece;
(3) according to required positive/negative plate size, use coated separator, be wound into battery core, then two battery cores swashing after linking shell Flush weld, fluid injection, chemical conversion, make battery.
CN201610780828.2A 2016-08-30 2016-08-30 High-safety long-life composite material system power battery and preparation method thereof Pending CN106328935A (en)

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Application publication date: 20170111