CN104538591B - Pre-lithiation method of lithium ion battery negative electrode material - Google Patents

Pre-lithiation method of lithium ion battery negative electrode material Download PDF

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CN104538591B
CN104538591B CN201410839836.0A CN201410839836A CN104538591B CN 104538591 B CN104538591 B CN 104538591B CN 201410839836 A CN201410839836 A CN 201410839836A CN 104538591 B CN104538591 B CN 104538591B
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lithium
lithium ion
collector
ion battery
barrier layer
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CN104538591A (en
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徐宁
梁运辉
高川
杨化滨
吴孟涛
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Tianjin B&M Science and Technology 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
    • H01M4/64Carriers or collectors
    • 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
    • H01M10/058Construction or manufacture
    • 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
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139Processes of manufacture
    • 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
    • H01M4/362Composites
    • 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
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • 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 Kinetics & Catalysis (AREA)
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  • General Chemical & Material Sciences (AREA)
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  • Composite Materials (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Secondary Cells (AREA)

Abstract

The invention discloses a pre-lithiation method of a lithium ion battery negative electrode material. The method is characterized in that by adopting a method of coating or covering the surface of metal lithium with a lithium ion barrier layer and/or controlling a resistance value of a connection conductor, the pre-lithiated current magnitude is limited, and the reaction speed of a primary battery between metal lithium and negative electrode materials is regulated so as to regulate the lithium-intercalation speed of the negative electrode material and formation speed of surface SEI films, and the circulation performance of the negative electrode material is improved based on the improvement on coulombic efficiency for the first time of the negative electrode material; moreover, the method is simple in process and easy to operate, and suitable for pre-lithiation of the commercial lithium ion battery negative electrode material; lithium consumed by irreversible reaction is supplemented, so that the coulombic efficiency for the first time and the capacity of the battery are increased, and the circulation performance of the battery is improved.

Description

The prelithiation method of lithium ion battery negative material
Technical field
The present invention relates to the prelithiation method field of lithium ion battery material, particularly to a kind of lithium ion battery negative material The prelithiation method of material.
Background technology
With the fast development of electronic product, high-energy, the demand of high power density lithium ion battery increase year by year, non-stone Inkization material with carbon element, oxide material and composite etc. receive much concern because of high power or high power capacity.However, such material exists not Reversible capacity is high, and the low serious problems of coulombic efficiency first are easily caused capacity of lithium ion battery and are decreased obviously.At present, in order to Coulombic efficiency is low first to solve the problems, such as lithium ion battery negative material, people developed chemical reduction method, artificial sei embrane method and Electrochemistry prelithiation method, wherein electrochemistry prelithiation method are that one kind the most directly solves the low storehouse first of lithium ion battery negative material The method of human relations efficiency.
In the patent of cn200480021793.x, disclose one kind by lithium and electrode material directly contact, then by former Cell reaction realizes the prelithiation method of electrode material.However, the method easily produces " dead lithium ", that is, the lithium adding can not be filled Divide and utilize;And lithium and electrode material directly contact can cause lithiumation electric current excessive, cause electrode material structural deterioration and densification And stable sei film difficult to form, ultimately result in the cycle performance decline of electrode material.
In the patent of cn200910188470.4, disclose one kind and by lithium deposition or snap non-dressing on a current collector Area, the method recycling galvanic interaction to realize electrode material prelithiation, improve the utilization rate of lithium, solve " dead lithium " and ask Topic.But, lithium is to be connected by the very little collector of resistance with electrode material, and lithiumation electric current will be very big, equally easily The cycle performance causing electrode material declines.
In the patent of cn201210573270.2, for the big problem of lithiumation electric current, disclose a kind of low temperature fluid injection side Method, makes galvanic interaction carry out at a lower temperature, controls the embedding lithium speed of material, thus improving material coulombic efficiency first While with capacity, improve the cycle performance of material.However, the method needs low-temperature operation, technique is more complicated, high cost, and And the electrolysis fluid viscosity under low temperature increases, fluid injection operating difficultiess.
Content of the invention
It is an object of the invention to provide a kind of process is simple, with low cost, prelithiation electric current can be efficiently controlled, carry The coulombic efficiency first of high negative material, and significantly improve the lithium ion battery negative material prelithiation side of its cycle performance Method.
For this reason, technical scheme is as follows:
A kind of prelithiation method of lithium ion battery negative material, comprises the steps:
(1) snapping the cladding of the metallic lithium surface on collector or superscribing lithium ion barrier layer, then be coated with bearing The collector of pole slurry is connected on described collector or described lithium metal by the conductor of resistance value r≤0.1 ω;
Or snapping the cladding of the metallic lithium surface part on collector or superscribing lithium ion barrier layer, then it is coated with The collector of cathode size 1 is by resistance value r > conductor of 0.1 ω is connected on described collector or described lithium metal;
Or snap lithium metal on a current collector, then it is coated with the collector of cathode size by resistance value r > 0.1 ω Conductor is connected on described collector or described lithium metal;
Wherein, described barrier layer does not dissolve in and is formed with least one micropore on electrolyte and described barrier layer;
(2) negative electrode processing through described step () and anelectrode are assembled into lithium ion battery.
(3) by the lithium ion battery standing activation of assembling in described step (two), formed between lithium metal and negative material Galvanic interaction, when reaction to lithium metal consumes completely, that is, completes the prelithiation of lithium ion battery negative material.
In step (), in metallic lithium surface cladding or to superscribe the effect of lithium ion barrier layer be limiting lithium ion Diffusion velocity;The effect of conductor is to build electronics path between lithium metal and negative pole to form galvanic element, limits prelithiation Size of current.Two methods are all conducive to adjusting the galvanic interaction speed between lithium metal and negative material, to be regulated and controled with this The embedding lithium speed of negative material and surface sei film form speed, thus the basis in the coulombic efficiency first improving negative material On, improve the cycle performance of negative material.
In step (), two kinds of prelithiation methods with conductor resistance value r=0.1 ω carry out description be because to lithium from Sub- battery carries out in short circuit safety energy testing experiment, and the conductor being typically less than 0.1 ω with resistance is tested, and in electricity During pond is actually used, conductor resistance should be greater than 0.1 ω.
The collector snapping lithium metal and be coated with cathode size collector can for identical metal or Different metal.
In step (three), lithium ion battery stands activation process, forms galvanic element between lithium metal and negative material React and consume completely process to lithium metal, this process can complete in the case of standing it is also possible to directly use in energising Complete in journey.
Preferably, the micropore size of porosity≤80% of described barrier layer, or barrier layer is not more than 5mm.By to not Quantity and micropore size with the micropore being formed on the barrier layer that material is made are controlled, can be to the diffusion speed of lithium ion Degree is adjusted.
Preferably, the material of described barrier layer is plastic foil, hard paraffin, Copper Foil or the micropore being not involved in electrochemical reaction Barrier film.Described barrier layer can also be able to be multilamellar for monolayer.
Preferably, described conductor by least one conductive metal or nonmetallic is made;It is highly preferred that leading described in making The metal of body or nonmetallic be all not involved in the reaction of embedding lithium.
Described conductor and described lithium ion barrier layer, they pass through resistance respectively and hole passes to electronics in prelithiation circuit Defeated and lithium ion transport limits, thus limiting prelithiation response speed.This is because in prelithiation reaction, electronics and lithium ion Both participate in galvanic interaction, limit either or both, all can limit prelithiation response speed.
Additionally, can also relatively efficiently regulate and control the prelithiation depth of negative material by the adjustment of the consumption to lithium metal, The i.e. degree of the raising of material initial coulomb efficiency.If the consumption of lithium metal exceedes the first week electrochemical reaction consumption of negative material Lithium and battery standing soak time long enough, then the open-circuit voltage of battery eventually drops to 0v, and the lithium metal of excess is then The lithium that during progressively discharging with replenishment cycles in follow-up cyclic process, irreversible reaction consumes, but negative material The improvement of initial coulomb efficiency and cycle performance is unaffected, and the coulombic efficiency of its later cycles will reach or slightly super Cross 100%.
The prelithiation method of this lithium ion battery negative material, by coating in metallic lithium surface or superscribing lithium ion resistance Interlayer and/or the method carrying out resistance value control to connection conductor, limit the size of current of prelithiation, adjust lithium metal and negative pole Galvanic interaction speed between material, and the embedding lithium speed to regulate and control negative material with this and surface sei film form speed, from And on the basis of the coulombic efficiency first improving negative material, improve the cycle performance of negative material;And the present invention is adopted Process is simple, easily operated, it is suitable for the prelithiation of commercial Li-ion battery negative material, supplement because of irreversible reaction The lithium consuming, thus improving the coulombic efficiency first of battery, capacity, and improves its cycle performance.
Brief description
Fig. 1 is the structural representation of negative material prelithiation electrode in embodiments of the invention 1;
Fig. 2 is the structural representation of negative material prelithiation electrode in embodiments of the invention 2;
Fig. 3 is the structural representation of negative material prelithiation electrode in the comparative example 2 of the present invention;
Fig. 4 is the structural representation of negative material prelithiation electrode in the comparative example 3 of the present invention;
When Fig. 5 is the comparative example 1~3 of the present invention and the open-circuit voltage of battery prepared by embodiment 1~2 and standing activation Between graph of a relation.
Specific embodiment
Below in conjunction with the accompanying drawings the prelithiation method of the lithium ion battery negative material of the present invention is described in detail, but this Invention is not limited solely to following examples.
As shown in Fig. 1~2, the prelithiation method of this lithium ion battery negative material, comprise the steps:
(1) in lithium metal 3 Surface coating snapping on collector 21 or superscribe lithium ion barrier layer 5, then will coat The collector 22 having cathode size 1 is connected to described collector 21 or described lithium metal 3 by the conductor 4 of resistance value r≤0.1 ω On;
Or in the lithium metal 3 surface portion cladding snapping on collector 21 or superscribe lithium ion barrier layer 5, then will apply The collector 22 being covered with cathode size 1 passes through resistance value r > conductor 4 of 0.1 ω is connected to described collector 21 or described lithium metal On 3;
Or lithium metal 3 is snapped on collector 21, then it is coated with the collector 22 of cathode size 1 by resistance value r > The conductor 4 of 0.1 ω is connected on described collector 21 or described lithium metal 3;
Wherein, described barrier layer 5 material does not dissolve in and is formed with least one micropore on electrolyte and described barrier layer 5;
(2) negative electrode processing through described step () and anelectrode are assembled into lithium ion battery.
(3) by the lithium ion battery standing activation of assembling in described step (two), formed between lithium metal and negative material Galvanic interaction, when reaction to lithium metal consumes completely, that is, completes the prelithiation of lithium ion battery negative material.
Wherein, porosity≤80% of described barrier layer.Described barrier layer 5 material is the plastics being not involved in electrochemical reaction Film, hard paraffin, Copper Foil or micro-pore septum.Described barrier layer 5 is single or multiple lift.Described conductor 4 can be conductive by least one Metal or nonmetallic make.The metal making described conductor 4 is not involved in embedding lithium reaction.
All using having good chemical property silicon-Si oxide-in example 1 below~4 and comparative example 1~3 Carbon compound cathode materials (method with reference to disclosed patent cn201310683767.4 is prepared from), as active material, are made 2032 type button cells, to assess the improvement to lithium ion battery negative material chemical property for the prelithiation method.Wherein, The cathode size 1 being coated on collector 22 by silicon-Si oxide-carbon compound cathode materials, conductive agent, pvdf with weight ratio is 8:1:1 forms, and metal lithium sheet is made to electrode, 1mol/l lipf6The solution of ec/dmc (volume ratio be 1:1) make electrolyte, Cellgard2400 micro-pore septum makees barrier film, and collector 21 and collector 22 are Copper Foil.
Embodiment 1
As shown in figure 1, having snapped thickness in copper foil current collector 21 is 0.1mm lithium metal thin layer, then it is coated with negative pole The cr that the copper foil current collector 22 of slurry 1 is 1 ω by resistance value20ni80Resistance wire is connected in described copper foil current collector 21, its In, the weight of lithium metal thin layer is the 10% of silicon-Si oxide-carbon compound cathode materials weight, then by through above-mentioned process Negative electrode and anelectrode are assembled into lithium ion battery, standing activation 24h.
Embodiment 2
As shown in Fig. 2 being 0.1mm lithium metal thin layer surface tight one snapping the thickness in copper foil current collector 21 Layer Copper Foil is as lithium ion barrier layer, and is punctured with the micropore that two apertures are 0.5mm on the Copper Foil as barrier layer, then will The copper foil current collector 22 being coated with cathode size 1 is connected to described copper foil current collector 21 by the copper wire of resistance value r=0.005 ω On, wherein, the weight of lithium metal thin layer is the 10% of silicon-Si oxide-carbon compound cathode materials weight, then will be through above-mentioned place The negative electrode of reason and anelectrode are assembled into lithium ion battery, standing activation 24h.
Embodiment 3
It is that one layer of paraffin of 0.1mm lithium metal thin layer 3 surface tight is made snapping the thickness in copper foil current collector 21 For lithium ion barrier layer, and the micropore that 1 aperture is 0.2mm is punctured with the paraffin as barrier layer, then is coated with bearing The copper foil current collector 22 of pole slurry 1 is connected in described copper foil current collector 21 by the copper wire of resistance value r=0.005 ω, wherein, The weight of lithium metal thin layer is the 10% of silicon-Si oxide-carbon compound cathode materials weight, then by the negative electricity through above-mentioned process Pole and anelectrode are assembled into lithium ion battery, standing activation 24h.
Embodiment 4
It is four layers of cellgard of tight on 0.1mm lithium metal thin layer snapping in the thickness in copper foil current collector 21 2400 micro-pore septums are as lithium ion barrier layer, then to be coated with the copper foil current collector 22 of cathode size 1 be 0.1 by resistance value The resistance wire of ω is connected in described copper foil current collector 21, and wherein, the weight of lithium metal thin layer is that silicon-Si oxide-carbon is combined Then negative electrode through above-mentioned process and anelectrode are assembled into lithium ion battery, standing activation by the 5% of negative material weight 24h.
Comparative example 1
The cathode size 1 being coated with silicon-Si oxide-carbon compound cathode materials preparation in copper foil current collector is as negative Pole, is assembled into lithium ion battery, standing activation 24h with anelectrode.
Comparative example 2
As shown in figure 3, coating in copper foil current collector 22 by the negative pole of silicon-Si oxide-carbon compound cathode materials preparation Slurry 1, and the lithium metal thin layer 3 that thickness is 0.1mm has been snapped on the part surface of affiliated negative material, lithium metal thin layer Weight is the 10% of silicon-Si oxide-carbon compound cathode materials weight, then by the negative electrode through above-mentioned process and anelectrode group Dress up lithium ion battery, standing activation 24h.
Comparative example 3
As shown in figure 4, uncoated silicon-Si oxide-carbon compound cathode materials are formed with copper foil current collector 22 obtaining not Dressing area, and the lithium metal thin layer that thickness is 0.1mm has been snapped on non-dressing area, its weight is that silicon-Si oxide-carbon is combined Then negative electrode through above-mentioned process and anelectrode are assembled into lithium ion battery, standing activation by the 10% of negative material weight 24h.
Performance test:
Coulombic efficiency test first:
The first charge-discharge coulombic efficiency of lithium ion battery can directly reflect the chemical property of this battery system, one As cell negative electrode material the low performance that can affect its corresponding positive electrode capacity of efficiency.Therefore first charge-discharge coulombic efficiency for Assessment battery performance plays a crucial role.
Coulombic efficiency test condition first to each embodiment and comparative example in this embodiment: room temperature condition Under, battery is carried out under the electric current density of 100ma/g constant current charge-discharge, voltage range is 0.01~3.0v, record battery is first Secondary coulombic efficiency.
Reversible capacity is tested:
To the cycle performance of battery, effective evaluation can be carried out to the reversible capacity test after circulating battery some cycles, its Reversible capacity after circulation some cycles is less with the difference of reversible capacity first, and its reversible capacity conservation rate is higher, i.e. energy Loss speed slower it was demonstrated that this battery usage cycles is longer.
After in this embodiment first all reversible capacities of each embodiment and comparative example being tested and are circulated for 100 weeks Reversible capacity test condition: under room temperature condition, battery is carried out under the electric current density of 100ma/g constant current charge-discharge, voltage model Enclose for 0.01~3.0v, and circulate 100 cycles, record battery first week reversible capacity and circulation in 100 weeks after reversible capacity, calculating Capability retention after circulation in 100 weeks.
The electrochemical property test result of 2032 type button cells prepared by table 1. comparative example 1~3 and embodiment 1~4:
Comparative example 2 and comparative example 3 are the existing schemes that negative material is carried out with prelithiation, can see compared with comparative example 1 Go out, coulombic efficiency and cycle performance first can be effectively improved by negative material is carried out with prelithiation.And compared with comparative example 2 The prelithiation method to negative material that comparative example 3 is adopted has more preferable cycle performance.
Embodiment 1~4 be technical solution of the present invention disclosed in prelithiation is carried out to improve coulomb first to negative material Efficiency and the specific embodiment of cycle performance.
Embodiment 1 is by snapping lithium metal on a current collector, then is coated with the collector of cathode size 1 and passes through resistance Value r > method that the conductor of 0.1 ω is connected on described collector or described lithium metal completes to carry out prelithiation to negative material. The method passes through the resistance value connecting conductor is defined reaching with the restriction to prelithiation electric current, that is, adjust lithium metal and bear Galvanic interaction speed between the material of pole.Compared with comparative example 3, its first coulombic efficiency be still maintained at more than 100%, no Loss;And after it circulates 100 weeks, reversible capacity only drops to 569.6mah/g by 623.7mah/g, its reversible capacity conservation rate For 91.3%, with respect to comparative example 3, there is more excellent cycle performance.
Embodiment 2~4 be by snap the metallic lithium surface on collector cladding or superscribe lithium ion barrier layer, The collector being coated with cathode size 1 again is connected to described collector or described metal by the conductor of resistance value r≤0.1 ω Method on lithium completes to carry out prelithiation to negative material.The method is arrived by the dissolution rate that lithium ion barrier layer limits lithium Reach the restriction to prelithiation electric current, that is, adjust the galvanic interaction speed between lithium metal and negative material.
Compared with comparative example 3, embodiment 2 adopt Copper Foil as lithium ion barrier layer, its first coulombic efficiency still keep More than 100%, free of losses;And reversible capacity only drops to 601.6mah/g by 607.0mah/g after it circulates 100 weeks, its Reversible capacity conservation rate is 99.1%, and that is, cycle performance of battery is obviously improved.
Compared with comparative example 3, embodiment 3 as lithium ion barrier layer and is punctured with two apertures thereon and is using paraffin The micropore of 0.5mm, its first coulombic efficiency be 81.5, have certain electricity damage, after its circulation 100 weeks reversible capacity by 626.5mah/g drops to 557.4mah/g, and its reversible capacity conservation rate is 89.9%, and that is, cycle performance of battery has also been lifted.
Compared with comparative example 3, on embodiment 4 lithium metal thin layer, four layers of cellgard 2400 micro-pore septum of tight are made For lithium ion barrier layer, its first coulombic efficiency be 98.0%, electric loss is less, after its circulation 100 weeks reversible capacity only by 620.8mah/g drops to 574.2mah/g, and its reversible capacity conservation rate is 92.5%, and that is, cycle performance of battery is effectively carried Rise.
In conjunction with Fig. 5, i.e. comparative example 1~3 and the open-circuit voltage of battery prepared by embodiment 1~2 and standing soak time Graph of a relation be analyzed it can be seen that realize the prelithiation of negative material using the embodiment of prelithiation method of the present invention, electricity The open-circuit voltage in pond declines slow, is conducive to negative material surface to form the stable and sei film of densification such that it is able to significantly improve Its cycle performance.
Negative active core-shell material, in addition to the novel silicon-Si oxide-carbon compound cathode materials adopting in an embodiment, also adopts Soft carbon and ferrum oxide etc. are as negative material, and carry out the preprocess method in embodiment such as and carry out pre- place to negative material Reason, has carried out electrochemical property test, it may have good result simultaneously, that is, has effectively improved coulombic efficiency and cycle performance first.

Claims (4)

1. a kind of prelithiation method of lithium ion battery negative material is it is characterised in that comprise the steps:
(1) in lithium metal (3) Surface coating snapping on collector (21) or parcel lithium ion barrier layer (5), then will coat The collector (22) having cathode size (1) is connected to described collector (21) or institute by the conductor (4) of resistance value r≤0.1 ω State on lithium metal (3);
Snap lithium metal (3) surface portion on collector (21) cladding or superscribe lithium ion barrier layer (5), then will Be coated with cathode size (1) collector (22) pass through resistance value r > 0.1 ω conductor (4) be connected to described collector (21) or On described lithium metal (3);Or lithium metal (3) is snapped on collector (21), then the collector being coated with cathode size (1) (22) passing through resistance value r > conductor (4) of 0.1 ω is connected on described collector (21) or described lithium metal (3);
Wherein, the material of described barrier layer (5) is not dissolved in that to be formed with least one on electrolyte and described barrier layer (5) micro- Hole;Porosity≤80% of described barrier layer (5);Described barrier layer (5) material is plastic foil, hard paraffin, Copper Foil or micropore Barrier film;
(2) negative electrode processing through described step () and anelectrode are assembled into lithium ion battery;
(3) by the lithium ion battery standing activation of assembling in described step (two), between lithium metal and negative material, form former electricity Pond is reacted, and when reaction to lithium metal consumes completely, that is, completes the prelithiation of lithium ion battery negative material.
2. the prelithiation method of lithium ion battery negative material according to claim 1 is it is characterised in that described barrier layer (5) it is single or multiple lift.
3. the prelithiation method of lithium ion battery negative material according to claim 1 is it is characterised in that described conductor (4) by least one conductive metal or nonmetallic make.
4. the prelithiation method of the lithium ion battery negative material according to claims 1 to 3 any one claim, it is special Levy and be, make the metal of described conductor (4) or nonmetallic be all not involved in the reaction of embedding lithium.
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