CN110190258A - Aqueous composite mortar of Si-C composite material and preparation method thereof, lithium ion battery - Google Patents

Aqueous composite mortar of Si-C composite material and preparation method thereof, lithium ion battery Download PDF

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CN110190258A
CN110190258A CN201910492163.9A CN201910492163A CN110190258A CN 110190258 A CN110190258 A CN 110190258A CN 201910492163 A CN201910492163 A CN 201910492163A CN 110190258 A CN110190258 A CN 110190258A
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composite material
preparation
slurry
aqueous
composite
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CN110190258B (en
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陈献武
李旺
詹吟桥
闫海
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Shanghai Electric Group Corp
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Shanghai Electric Group Corp
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    • 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
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/362Composites
    • H01M4/364Composites as mixtures
    • 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
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • 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
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/386Silicon or alloys based on silicon
    • 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
    • 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

Abstract

The invention discloses aqueous composite mortars of a kind of Si-C composite material and preparation method thereof, lithium ion battery.It includes the following steps: that Si-C composite material and SP, which are 1. carried out dry powder, stirs to obtain material A;2. material A, water and CMC colloid, which are carried out infiltration, stirs to obtain slurry, solid content is 40~45%;3. after slurry, SBR emulsion and PAA lotion are carried out moderate-speed mixer, deaeration is stood;4. adjusting viscosity is 2000~3000mPas.Aqueous compound binding agent slurry of the invention takes water as a solvent, it is uniformly dispersed, the time of secondary agitation is shortened in its preparation process, binder distributing homogeneity on pole piece can be effectively improved, the effective decomposition for inhibiting electrolyte in cyclic process, more uniform SEI film is formed, coulombic efficiency is high for the first time for thus obtained lithium ion battery, good cycle.

Description

Aqueous composite mortar of Si-C composite material and preparation method thereof, lithium ion battery
Technical field
The present invention relates to aqueous composite mortars of a kind of Si-C composite material and preparation method thereof, lithium ion battery.
Background technique
In recent years, as increasingly reducing for fossil energy is increasingly serious with environmental problem, lithium ion battery is in electronic vapour The application of vehicle and energy storage field has been to be concerned by more and more people.Due to lithium ion battery relative to other type cells have compared with High energy density and power density, it is considered to be current most promising electrical energy storage device.However, existing lithium-ion electric The energy density and power density in pond are still relatively low, and the following electric car and energy storage system has not yet been reached in safety and cycle life The requirement of system application.
Graphite negative electrodes material has been widely used in lithium since it is with high cycle efficieny and good cycle performance The production of ion battery.But its lithium storage content is lower, theoretical specific capacity 372mAh/g, and intercalation potential is electric close to lithium metal Position, in high power charging-discharging, there are still security risks, therefore develop heat of the novel anode material as the current research field Point, the research of high-capacity cathode material at present is concentrated mainly on Si, Sn, Sb, Al and Pb etc. can be with the gold of Li electrochemically alloying Belong to, the amount of the reversible embedding de- Li of such alloy anode is far longer than graphite, such as the theoretical specific capacity of silicon (Si) base negative electrode material Up to 4200mAh/g, along with the advantages such as its low intercalation potential, low cost are generally considered next-generation negative electrode of lithium ion battery Material.
The theoretical specific capacity (4200mAh/g) of silicon (Si) base negative electrode material is high, embedding de- lithium platform is convenient, is a kind of ideal Lithium ion battery high-capacity cathode material.However, in charge and discharge process, i.e., during removal lithium embedded, the volume of silicon materials It changes greatly (volume expansion is up to 400%), internal stress caused by violent volume change, is easy to cause silicon particle rupture point Change, so that silicon particle and conductive network is taken off lithium (electrode dusting is peeled off), internal resistance increases, and causes reversible capacity to be decayed rapidly, cyclicity It can sharp fall.
In lithium ion battery, binder be influence electrode structure stability an important factor for one of.According to decentralized medium Property, lithium ion battery binder can be divided into using organic solvent as the oiliness binder of dispersing agent and using water as the water of dispersing agent Property binder.
CN102916190A discloses a kind of aqueous slurry for battery electrode, such as public affairs in the 12nd section of the 4th row of specification It opens, PVDF can be used for water-based slurry, thus in the chemistry and electrochemistry advantage that keep PVDF.In the 13rd~16 section of specification Open, mainly by PVDF in aqueous binders use, enables PVDF in aqueous solvent by some ameliorative ways Lower use, and some advantages of aqueous binders can be inherited, not disclosing slurry group becomes the technology of PAA+SBR+CMC Scheme.According to common sense in the field it is found that usually under the conditions of aqueous solvent (referring generally to deionized water), PVDF is not dissolved simultaneously, should It is used using PAA or SBR as the solvent of PVDF in patent application, PVDF is used as laminated dose (disclosing in such as the 13rd section) and makes With, and general silica-base material (SiOx and graphite composite material) usually only uses aqueous solvent.And it does not disclose SBR cream Liquid is preparing slurry technique, if it in mixing time longer process, there is demulsifying phenomenon, i.e. too long its of mixing time glues Property decline, cannot be used well as the effect of binder.
Summary of the invention
The present invention is poor, the Bu Nengying that overcomes SBR emulsion self-strength in the prior art practical the technical issues of solving The defect of Si matrix based material for high volume expansion provides a kind of aqueous composite mortar of Si-C composite material and its preparation Method, lithium ion battery.Aqueous compound binding agent slurry of the invention takes water as a solvent, and is uniformly dispersed, contracts in preparation process The short time of secondary agitation, it can be effectively improved binder distributing homogeneity on pole piece, it is effective to inhibit in cyclic process The decomposition of electrolyte forms more uniform SEI film, and coulombic efficiency is high for the first time for thus obtained lithium ion battery, cycle performance It is good.
The present invention solves above-mentioned technical problem by the following technical programs.
The present invention provides a kind of preparation methods of the aqueous composite mortar of Si-C composite material comprising following step:
1) Si-C composite material and conductive black (SP) are subjected to dry powder stirring, obtain material A;
2) material A, water and sodium carboxymethylcellulose colloid are subjected to infiltration stirring, obtain slurry, the solid content of the slurry It is 40~45%;
3) after the slurry, SBR emulsion (SBR) and polyacrylate emulsion (PAA) being carried out moderate-speed mixer, deaeration, It stands;
4) adjusting viscosity is 2000~3000mPas.
In the present invention, preferably, the raw material of the aqueous composite mortar of the Si-C composite material is than water by following components Composition: Si-C composite material, conductive black, sodium carboxymethylcellulose, butadiene-styrene rubber and polyacrylic acid.
In step 1), the Si-C composite material is generally powdered.The type of the Si-C composite material can be ability Domain is conventional.Currently, commercialized Si-C composite material will mainly aoxidize sub- silicon and nano-silicon respectively with the compound gained of graphite.It is logical The silicon materials that addition mass fraction is 5%~10% are crossed, the reversible capacity of gained Si-C composite material is up to 450-650mAh/ G, coulombic efficiency, cycle performance, in terms of can partially meet application requirement, in consumer electronics and electric car etc. It is gradually applied in field.In the present invention, the capacity of the Si-C composite material is generally 450~650mAh/g.
In step 1), the conductive black can be the conductive black of this field conventional commercial.
In step 1), the operation of the dry powder stirring and condition can be conventional for this field, generally stirred using planet rotor Machine carries out.The revolution speed of the dry powder stirring is preferably 1800~2200r/min, such as 2000r/min.The dry powder stirs The time mixed is preferably 25~35min, is more preferably 30min.
In step 2), the sodium carboxymethylcellulose colloid is generally sodium carboxymethylcellulose powder and is dissolved in the water to be formed Colloid.The concentration of the sodium carboxymethylcellulose colloid can be conventional for this field, and preferably 2~5%.
In step 2), the operation of the infiltration stirring and condition can be conventional for this field, generally stirred using planet rotor Machine carries out.The revolution speed of the infiltration stirring is preferably 500~2000r/min, such as 500r/min, 1000r/min, 1500r/min or 2000r/min.The time of the infiltration stirring is preferably 10~30min, such as 20min.
In step 2), the water can be water commonly used in the art, generally deionized water.The dosage of the water is general It is determined according to the solid content of slurry.According to common sense in the field it is found that the solid content=(Si-C composite material+conduction charcoal Black+sodium carboxymethylcellulose+binder)/(Si-C composite material+conductive black+sodium carboxymethylcellulose+binder+deionization Water).
In step 3), preferably, after the SBR emulsion and polyacrylate emulsion are premixed again with the slurry Material mixing.The operation of the premix and condition can be conventional for this field.
In step 3), the SBR emulsion can be this field conventional commercial product.The SBR emulsion is consolidated Content can be conventional for this field, such as 40~60%.In a certain embodiment, the solid content of SBR emulsion can be 50%.
In step 3), the polyacrylate emulsion can be this field conventional commercial product.The polyacrylate emulsion is consolidated Content can be conventional for this field, such as 20~40%.In a certain embodiment, the solid content of polyacrylate emulsion can be 30%.
In step 3), if SBR emulsion mixing time is longer, there is demulsifying phenomenon, i.e. too long its of mixing time glues Property decline, cannot use well as binder.Only within the scope of the above-mentioned special process of the present invention, SBR cream just can guarantee Liquid plays its effect, just can solve technical problem of the invention.
In step 3), the operation of the moderate-speed mixer and condition can be conventional for this field.The revolution speed of the moderate-speed mixer Spend preferably 900~1300rpm, more preferably 1000~1200rpm.The time of the moderate-speed mixer preferably 3~5min.If stirring Overlong time is mixed, binder viscosity can decline, and subsequent coating can not carry out, and there is pole piece phenomenons.
In the present invention, the Si-C composite material, the conductive black, the sodium carboxymethylcellulose, the butylbenzene rubber Glue SBR, the polyacrylic acid PAA mass ratio can be conventional for this field, preferably (85~93): (2~5): (2~4): (2 ~4): (2~4).
In the present invention, when the capacity of the Si-C composite material is 650mAh/g, the Si-C composite material described is led Electric carbon black, the sodium carboxymethylcellulose, the butadiene-styrene rubber, the polyacrylic acid mass ratio be preferably 85: 5: 4: 3: 3。
In the present invention, when the capacity of the Si-C composite material is 450mAh/g, the Si-C composite material described is led Electric carbon black, the sodium carboxymethylcellulose, the butadiene-styrene rubber, the polyacrylic acid mass ratio can be 93: 2: 2: 1.5: 1.5。
In step 3), the operation of the deaeration and condition can be conventional for this field.The revolution speed of the deaeration is generally 1000~1200r/min, inclined heated plate are generally 1~2min.
In step 3), the operation of the standing and condition can be conventional for this field.The time of the standing is generally 1~ 5min, preferably 2min.
In step 4), according to common sense in the field, water regulation system viscosity is generally used.
In step 4), according to common sense in the field, after generally having adjusted system viscosity, vacuum is stood, after bubble removing coating be It can.
The present invention also provides the aqueous composite mortars of one kind Si-C composite material as made from above-mentioned preparation method.
It is aqueous compound that above-mentioned Si-C composite material is coated with the present invention also provides a kind of lithium ion battery, in negative electrode tab Slurry.
On the basis of common knowledge of the art, above-mentioned each optimum condition, can any combination to get each preferable reality of the present invention Example.
The reagents and materials used in the present invention are commercially available.
The positive effect of the present invention is that:
The preparation method of the aqueous composite mortar of Si-C composite material of the present invention is easy, and preparation total time is 45min or so, behaviour Make convenient controllable, it can be achieved that industrial applications produce;Gained slurry good dispersion.The slurry can be effectively improved adhesive particle The distributing homogeneity in pole piece can be used for the biggish silicon-carbon cathode system of volume change, restrained effectively electrode material de- Volumetric expansion in process of intercalation reduces the decomposition of electrolyte, improves in cyclic process pole piece during removal lithium embedded The stability of the SEI film formed in volume expansion;The cycle performance of lithium ion battery as made from the slurry is good, for the first time coulombic efficiency It is high.
Detailed description of the invention
Fig. 1 is first charge-discharge curve graph of the slurry under 0.5C multiplying power made from embodiment 1.
Fig. 2 is first charge-discharge curve graph of the slurry under 0.5C multiplying power made from comparative example 1.
Fig. 3 is first charge-discharge curve graph of the slurry under 0.5C multiplying power made from comparative example 2.
Fig. 4 is that the cycle performance using battery made from embodiment 1,1~2 gained slurry of comparative example under 0.5C multiplying power is surveyed Try curve graph.
Fig. 5 is that the cycle performance using battery made from embodiment 2,3 gained slurry of comparative example under 0.5C multiplying power is tested Curve graph.
Specific embodiment
The present invention is further illustrated below by the mode of embodiment, but does not therefore limit the present invention to the reality It applies among a range.In the following examples, the experimental methods for specific conditions are not specified, according to conventional methods and conditions, or according to quotient The selection of product specification.
Raw material Si-C composite material used by Examples 1 to 3 and comparative example 1,2 will mainly aoxidize sub- silicon and nano-silicon Respectively with the compound acquisition of graphite, by addition mass fraction be 5%~10% silicon materials, the reversible appearance of Si-C composite material It measures up to 450-650mAh/g.Above-mentioned raw materials Si-C composite material can be by commercially available.
Embodiment 1
The preparation of the aqueous composite mortar of Si-C composite material:
1) take powdered Si-C composite material (650mAh/g) 1.7g, conductive black 0.1g using planet rotor blender It carries out dry powder and stirs 30min;Wherein, revolution speed 2000r/min;
2) to through deionized water 1.3g and sodium carboxymethylcellulose colloid 1.6g is added in step (1) mixed dry powder (content 5%), the infiltration stirring 20min in planet rotor blender obtain uniform just road slurry, control total solid and contain Amount ratio is 45% or so;Wherein, the revolution speed for infiltrating stirring is 1500r/min;
3) SBR emulsion 0.12g (content 50%) and polypropylene are continuously added into the slurry after infiltrated stirring The mixed emulsion of yogurt liquid 0.2g (content 30%) carries out middling speed short time mixing and the deaeration 2min (revolution speed of deaeration For 1000-1200r/min), 2min is stood;During middling speed short time mixing, revolution speed 1200r/min, time 5min;
Si-C composite material, conductive black, sodium carboxymethylcellulose, styrene butadiene rubber sbr, polyacrylic acid PAA mass ratio For 85:5:4:3:3;
4) slurry after middling speed short time mixing being adjusted into its viscosity to 2000~3000mPas, vacuum standing, gas removal steeps, Coating.
Embodiment 2
The preparation of the aqueous composite mortar of Si-C composite material:
1) powdered Si-C composite material (capacity 450mAh/g) 3.72g, conductive black 0.08g is taken to turn using planet Sub- blender carries out dry powder and stirs 25min;Wherein, revolution speed 2200r/min;
2) to through deionized water and sodium carboxymethylcellulose colloid 1.6g (content are added in step (1) mixed dry powder For 5%), the infiltration stirring 30min in planet rotor blender obtains uniform just road slurry, controls total solid content ratio Example is 45% or so;Wherein, the revolution speed for infiltrating stirring is 1000r/min;
3) SBR emulsion 0.12g (content 60%) and polypropylene are continuously added into the slurry after infiltrated stirring The mixed emulsion of yogurt liquid 0.2g (content 30%) carries out middling speed short time mixing and the deaeration 1min (revolution speed of deaeration For 1000-1200r/min), 1min is stood;During middling speed short time mixing, revolution speed 1200r/min, time 5min;
Si-C composite material, conductive black, sodium carboxymethylcellulose, styrene butadiene rubber sbr, polyacrylic acid PAA mass ratio For 93:2:2:1.5:1.5.
4) slurry after middling speed short time mixing being adjusted into its viscosity to 2000~3000mPas, vacuum standing, gas removal steeps, Coating.
Comparative example 1
The preparation of the aqueous composite mortar of Si-C composite material:
1) take powdered Si-C composite material (capacity 650mAh/g) 1.7g, conductive black 0.1g using planet rotor Blender carries out dry powder and stirs 30min;Wherein, revolution speed 2000r/min;
2) to through deionized water 1.3g and sodium carboxymethylcellulose colloid 1.6g is added in step (1) mixed dry powder (content 5%), the infiltration stirring 20min in planet rotor blender obtain uniform just road slurry, control solid content ratio Example is 45% or so;Wherein, the revolution speed for infiltrating stirring is 1500r/min;
3) it is continuously added into the slurry after infiltrated stirring SBR emulsion 0.24g (content 50%), in progress Fast short time mixing and deaeration 2min (revolution speed of deaeration is 1200r/min), stand 2min;Middling speed short time mixing process In, revolve 1200r/min, time 5min;
4) slurry after middling speed short time mixing being adjusted into its viscosity to 2000~3000mPas, vacuum standing, gas removal steeps, Coating.
Comparative example 2
1) take powdered Si-C composite material (capacity 650mAh/g) 1.7g, conductive black 0.1g using planet rotor Blender carries out dry powder and stirs 30min;Wherein, revolution speed 2000r/min;
2) to through deionized water 1.3g and sodium carboxymethylcellulose colloid 1.6g is added in step (1) mixed dry powder (content 5%), the infiltration stirring 20min in planet rotor blender obtain uniform just road slurry, control solid content ratio Example is 45% or so;Wherein, the revolution speed for infiltrating stirring is 1500r/min;
3) polyacrylate emulsion 0.4g (content 30%) is continuously added into the slurry after infiltrated stirring carries out middling speed Short time mixing and deaeration 2min (revolution speed of deaeration is 1200r/min), stand 2min;During middling speed short time mixing, Revolve 1200r/min, time 5min;
4) slurry after middling speed short time mixing is adjusted into its viscosity to 2000-3000mPas, vacuum standing, gas removal bubble applies Cloth.
Comparative example 3
The preparation of the aqueous composite mortar of Si-C composite material:
1) powdered Si-C composite material (capacity 450mAh/g) 3.72g, conductive black 0.08g is taken to turn using planet Sub- blender carries out dry powder and stirs 35min;Wherein, revolution speed 1800r/min;
2) to through deionized water and sodium carboxymethylcellulose colloid 1.6g (content are added in step (1) mixed dry powder For 5%), the infiltration stirring 10min in planet rotor blender obtains uniform just road slurry, controls total solid content ratio Example is 45% or so;Wherein, the revolution speed for infiltrating stirring is 2000r/min;
3) it is continuously added into the slurry after infiltrated stirring SBR emulsion 0.24g (content 50%), in progress Fast short time mixing and deaeration 2min (revolution speed of deaeration is 1000-1200r/min), stand 2min;Middling speed short time mixing In the process, revolution speed 1000r/min, time 3min;
Si-C composite material, conductive black, sodium carboxymethylcellulose, styrene butadiene rubber sbr mass ratio be 93:2:2:3.
4) slurry after middling speed short time mixing being adjusted into its viscosity to 2000~3000mPas, vacuum standing, gas removal steeps, Coating.
Effect example
By the electrochemistry of Si-C composite material composite binder cell size made from Examples 1 to 2, comparative example 1~3 Energy test process is as follows:
Cell size prepared by embodiment 1 is coated on copper foil of affluxion body.With 1.0mol/L LiPF6/ EC+DMC (body Product than 1:1)+VC+FEC (1%:10%) be electrolyte, Li piece be cathode, the U.S. produce Cellgard-2400 type polypropylene screen be Diaphragm is assembled into CR2032 type button cell in the glove box full of argon gas.Then in Wuhan City, blue electric electronics share is limited To material progress cycle performance of battery test is prepared on the CT2001A type battery test system of company's production, with the multiplying power of 0.5C Button type battery carries out charge and discharge.
Cell size prepared by embodiment 2, comparative example 1~3 is according to method preparation CR2032 type button electricity as shown above Pond and corresponding test.
Fig. 1 is first charge-discharge curve graph of the slurry under 0.5C multiplying power made from embodiment 1.As shown in Figure 1, it puts for the first time Capacitance is 843mAh/g, and initial charge capacity is 695.9mAh/g, first charge discharge efficiency 82.5%.Electricity obtained by embodiment 1 The discharge capacity for the first time of the battery performance of pond slurry is obviously improved, while coulombic efficiency improves for the first time.
Fig. 2 is first charge-discharge curve graph of the slurry under 0.5C multiplying power made from comparative example 1.As shown in Figure 2, it puts for the first time Capacitance is 805mAh/g, and initial charge capacity is 679.5mAh/g, first charge discharge efficiency 84%.
Fig. 3 is first charge-discharge curve graph of the slurry under 0.5C multiplying power made from comparative example 2.From the figure 3, it may be seen that putting for the first time Capacitance is 827.4mAh/g, and initial charge capacity is 683.2mAh/g, first charge discharge efficiency 82%.
Fig. 4 is that the cycle performance using battery made from embodiment 1,1~2 gained slurry of comparative example under 0.5C multiplying power is surveyed Try curve graph.As shown in Figure 4, cell size obtained by embodiment 1 can be effectively improved the cycle performance of battery.
Fig. 5 is that the cycle performance using battery made from embodiment 2,3 gained slurry of comparative example under 0.5C multiplying power is tested Curve graph.As shown in Figure 5, cell size obtained by embodiment 2 can be effectively improved the cycle performance of battery.
The electrochemical data of Examples 1 to 2,1~3 resulting materials of comparative example under 0.5C multiplying power is enumerated such as table 1.
Table 1

Claims (10)

1. a kind of preparation method of the aqueous composite mortar of Si-C composite material, which is characterized in that it includes the following steps:
1) Si-C composite material and conductive black are subjected to dry powder stirring, obtain material A;
2) material A, water and sodium carboxymethylcellulose colloid are subjected to infiltration stirring, obtain slurry, the solid content of the slurry is 40 ~45%;
3) after the slurry, SBR emulsion and polyacrylate emulsion being carried out moderate-speed mixer, deaeration is stood;
4) adjusting viscosity is 2000~3000mPas.
2. the preparation method of the aqueous composite mortar of Si-C composite material as described in claim 1, which is characterized in that the silicon-carbon It is grouped as than water by following groups in the raw material of the aqueous composite mortar of composite material: Si-C composite material, conductive black, carboxylic first Base sodium cellulosate, butadiene-styrene rubber and polyacrylic acid.
3. the preparation method of the aqueous composite mortar of Si-C composite material as described in claim 1, which is characterized in that the silicon-carbon The capacity of composite material is 450~650mAh/g;
And/or in step 1), the revolution speed of the dry powder stirring is 1800~2200r/min, such as 2000r/min;It is described The time of dry powder stirring is 25~35min, such as 30min.
4. the preparation method of the aqueous composite mortar of Si-C composite material as described in claim 1, which is characterized in that step 2) In, the concentration of the sodium carboxymethylcellulose colloid is 2~5%;
And/or in step 2), the revolution speed of the infiltration stirring is 500~2000r/min;
And/or in step 2), the time of the infiltration stirring is 10~30min.
5. the preparation method of the aqueous composite mortar of Si-C composite material as claimed in claim 4, which is characterized in that step 2) In, revolution speed 500r/min, 1000r/min, 1500r/min or 2000r/min of the infiltration stirring;
And/or in step 2), the time of the infiltration stirring is 20min.
6. the preparation method of the aqueous composite mortar of Si-C composite material as described in claim 1, which is characterized in that step 3) In, it is mixed again with the slurry after the SBR emulsion and polyacrylate emulsion are premixed;
And/or in step 3), the solid content of the SBR emulsion is 40~60%;
And/or in step 3), the solid content of the polyacrylate emulsion is 20~40%;
And/or in step 3), the revolution speed of the moderate-speed mixer is 900~1300rpm;
And/or in step 3), the time of the moderate-speed mixer is 3~5min.
7. the preparation method of the aqueous composite mortar of Si-C composite material as claimed in claim 6, which is characterized in that step 3) In, the solid content of the SBR emulsion is 50%;
And/or in step 3), the solid content of the polyacrylate emulsion is 30%;
And/or in step 3), the revolution speed of the moderate-speed mixer is 1000~1200rpm.
8. the preparation method of the aqueous composite mortar of Si-C composite material as described in claim 1, which is characterized in that the silicon-carbon Composite material, the conductive black, the sodium carboxymethylcellulose, the butadiene-styrene rubber, the polyacrylic acid mass ratio be (85~93): (2~5): (2~4): (2~4): (2~4);
When the capacity of the Si-C composite material is 650mAh/g, the Si-C composite material, the conductive black, the carboxylic Sodium carboxymethylcellulose pyce, the butadiene-styrene rubber, the polyacrylic acid mass ratio be 85:5:4: 3:3 or 93:2:2:1.5:1.5;
When the capacity of the Si-C composite material is 450mAh/g, the Si-C composite material, the conductive black, the carboxylic Sodium carboxymethylcellulose pyce, the butadiene-styrene rubber, the polyacrylic acid mass ratio be 93:2:2:4:2.
9. the aqueous composite mortar of Si-C composite material made from a kind of preparation method as described in any one of claims 1 to 8.
10. a kind of lithium ion battery, the aqueous composite mortar of Si-C composite material as claimed in claim 9 is coated in negative electrode tab.
CN201910492163.9A 2019-06-06 2019-06-06 Silicon-carbon composite material water-based composite slurry, preparation method thereof and lithium ion battery Active CN110190258B (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111816879A (en) * 2020-07-27 2020-10-23 日照广大建筑材料有限公司 Lithium ion battery cathode binder, slurry and cathode material thereof
CN112447960A (en) * 2020-12-01 2021-03-05 浙江锋锂新能源科技有限公司 Process method of composite binder in silicon cathode and preparation method of lithium ion battery
CN112563483A (en) * 2020-12-14 2021-03-26 广西卓能新能源科技有限公司 Positive active material slurry of lithium ion battery and preparation method

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102005562A (en) * 2010-09-30 2011-04-06 东莞新能源科技有限公司 Lithium ion battery and manufacturing method thereof
CN103872288A (en) * 2014-03-17 2014-06-18 山东润峰集团新能源科技有限公司 Preparation method for lithium ion battery negative electrode slurry
CN106058259A (en) * 2016-01-21 2016-10-26 万向A二三系统有限公司 High-specific-capacity silicon-based negative electrode composite binder and preparation method for negative plate containing same
CN106159266A (en) * 2016-08-31 2016-11-23 合肥国轩高科动力能源有限公司 A kind of cathode size preparation method reducing lithium ion battery expansion
CN109309232A (en) * 2018-09-13 2019-02-05 深圳市电科电源股份有限公司 A kind of preparation method of lithium ion battery with high energy density
CN109473626A (en) * 2017-09-07 2019-03-15 现代自动车株式会社 Electrode slurry and the electrode and lithium secondary battery for including the electrode slurry
CN109888264A (en) * 2019-04-20 2019-06-14 枣庄市产品质量监督检验所 A kind of high-energy cathode of lithium battery slurry and preparation method thereof

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102005562A (en) * 2010-09-30 2011-04-06 东莞新能源科技有限公司 Lithium ion battery and manufacturing method thereof
CN103872288A (en) * 2014-03-17 2014-06-18 山东润峰集团新能源科技有限公司 Preparation method for lithium ion battery negative electrode slurry
CN106058259A (en) * 2016-01-21 2016-10-26 万向A二三系统有限公司 High-specific-capacity silicon-based negative electrode composite binder and preparation method for negative plate containing same
CN106159266A (en) * 2016-08-31 2016-11-23 合肥国轩高科动力能源有限公司 A kind of cathode size preparation method reducing lithium ion battery expansion
CN109473626A (en) * 2017-09-07 2019-03-15 现代自动车株式会社 Electrode slurry and the electrode and lithium secondary battery for including the electrode slurry
CN109309232A (en) * 2018-09-13 2019-02-05 深圳市电科电源股份有限公司 A kind of preparation method of lithium ion battery with high energy density
CN109888264A (en) * 2019-04-20 2019-06-14 枣庄市产品质量监督检验所 A kind of high-energy cathode of lithium battery slurry and preparation method thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
郑仕琦: "高比容量硅碳负极的电极结构构筑", 《中国优秀硕士学位论文全文数据库 (工程科技Ⅱ辑)》 *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111816879A (en) * 2020-07-27 2020-10-23 日照广大建筑材料有限公司 Lithium ion battery cathode binder, slurry and cathode material thereof
CN111816879B (en) * 2020-07-27 2021-11-16 日照广大建筑材料有限公司 Lithium ion battery cathode binder, slurry and cathode material thereof
CN112447960A (en) * 2020-12-01 2021-03-05 浙江锋锂新能源科技有限公司 Process method of composite binder in silicon cathode and preparation method of lithium ion battery
CN112447960B (en) * 2020-12-01 2022-02-18 浙江锋锂新能源科技有限公司 Preparation method of silicon cathode and preparation method of lithium ion battery
CN112563483A (en) * 2020-12-14 2021-03-26 广西卓能新能源科技有限公司 Positive active material slurry of lithium ion battery and preparation method

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