CN104716312B - Silicon-carbon composite material for lithium ion battery, preparation method and application of silicon-carbon composite material - Google Patents

Silicon-carbon composite material for lithium ion battery, preparation method and application of silicon-carbon composite material Download PDF

Info

Publication number
CN104716312B
CN104716312B CN201510106478.7A CN201510106478A CN104716312B CN 104716312 B CN104716312 B CN 104716312B CN 201510106478 A CN201510106478 A CN 201510106478A CN 104716312 B CN104716312 B CN 104716312B
Authority
CN
China
Prior art keywords
composite material
carbon
silicon
silica flour
viscosity
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201510106478.7A
Other languages
Chinese (zh)
Other versions
CN104716312A (en
Inventor
郭玉国
孔鸣
孔一鸣
徐泉
殷雅侠
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Beijing One Gold Amperex Technology Ltd
Original Assignee
Institute of Chemistry CAS
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Institute of Chemistry CAS filed Critical Institute of Chemistry CAS
Priority to CN201510106478.7A priority Critical patent/CN104716312B/en
Publication of CN104716312A publication Critical patent/CN104716312A/en
Application granted granted Critical
Publication of CN104716312B publication Critical patent/CN104716312B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139Processes of manufacture
    • H01M4/1393Processes of manufacture of electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
    • 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
    • H01M4/1395Processes of manufacture of electrodes based on metals, Si 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
    • 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

Landscapes

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

Abstract

The invention provides a silicon-carbon composite material for a lithium ion battery, a preparation method and application of the silicon-carbon composite material. The silicon-carbon composite material for the lithium ion battery is 0.7-1.1 g/cm<3> in tap density, and is prepared from a porous silicon-carbon composite material and carbon filled in pores, wherein the silicon content in the porous silicon-carbon composite material is 10-40%, and the carbon content is 60-90%. The composite material is low in cost, high in practicability, and capable of being prepared in large scale; the composite material is high in tap density, and meanwhile multiple buffer layers are arranged, so that the problem that the silicon-based material as a lithium ion battery cathode material is poor in circulation can be solved.

Description

A kind of Silicon-carbon composite material for lithium ion battery and its preparation method and application
Technical field
The present invention relates to a kind of preparation method of Si-C composite material and its application as lithium ion battery negative material.
Background technology
With petroleum resources worsening shortages and environmental pollution it is increasingly severe, develop reproducible clean energy resource and increasingly weigh Will.The research and development of electric automobile have become one of global focus at present, and wherein lithium ion battery is used as its core technology Extremely pay attention to.There are lithium ion battery the outstanding advantages such as specific energy height, long service life, green non-pollution to be widely used In portable electronic products and electric automobile.At present business-like lithium ion battery negative material is mainly material with carbon element, but its Theoretical specific capacity is only 372mAh/g, cannot increasingly meet requirement of the lithium ion battery applications field to high-power, high power capacity. Therefore, the new type lithium ion battery for developing height ratio capacity is extremely urgent with negative material.
Silicon has high theoretical specific capacity (4200mAh/g) and removal lithium embedded, and being used as lithium ion battery negative most has prospect One of material, and rich reserves, cost are relatively low in the earth.But silicon materials adjoint serious body during removal lithium embedded Product change (~300%), causes the destruction and efflorescence of material structure, and then causes electrode cracking with active material from collector Come off, after repeatedly circulating, capacity is decayed rapidly, limits application of the silicon materials in field of lithium ion battery.Therefore, how to improve The cyclical stability of silicon materials, is the focus and emphasis of current research.
At present, mainly by the nanosizing of silicon and silicon based composite material improving the cyclical stability of silicon.But silicon nanometer Line, nano-tube preparation process are complicated, yield poorly, it is difficult to which industrialization large-scale production, degree of being practical are low.Due to carbons material With preferable flexible, good electron conduction, less volumetric expansion, and can be had by the cushion that carbon matrix is formed The volumetric expansion of the alleviation silicon materials of effect, improves the cyclical stability of silicon class material.
The content of the invention
The technical problem to be solved is to overcome that existing Si-C composite material first circle coulombic efficiency is low, circulation is steady Qualitative difference, high cost, preparation technology are not suitable for the defect of industrialized production.There is provided a kind of low cost, tap density it is high, can be big Silicon-carbon composite material for lithium ion battery of large-scale production and preparation method thereof, and effectively solved by multi-buffering-layer The defect of silicon class material, improves the cyclical stability of Si-C composite material.
The present invention improves a kind of Silicon-carbon composite material for lithium ion battery first, with higher tap density, vibration density Spend for 0.7-1.1g/cm3, it is made up of with the carbon being filled in its hole porous Si-C composite material, porous carbon-silicon composite material Middle silicone content is 10%-40%, and carbon content is 60%-90%.Preferably, the silicon face in porous Si-C composite material is coated Amorphous carbon or alundum (Al2O3).
Silicon-carbon composite material for lithium ion battery provided by the present invention is to prepare in accordance with the following steps:
1) by sanded treatment after silica flour ball mill grinding, the silica flour after process is dispersed in into macromolecule polymer solution or containing aluminium It is in the solution or the colloid containing silicon source in source and ultrasonically treated, make silica flour suspend in the solution, prevent to reunite.
2) by step 1) obtained by solution decompression rotary evaporation remove solvent after, be sintered under non-oxidizing atmosphere, The thickness of amorphous carbon or alundum (Al2O3), amorphous carbon or alundum (Al2O3) is coated for 5-30nm, content in silicon face For 0.5%-10%.
3) by step 2) obtained by the silica flour that coats with inorganic carbon source, hydroxy compounds dispersant, weight average molecular weight be The polymeric additive of 50000-400000 carries out mechanical agitation, is uniformly mixed, the suitable weak solution of viscosity.
4) by step 3) obtained by weak solution carry out spray drying treatment, obtain Si-C composite material, and non-oxidizable Be sintered under atmosphere, obtain the Si-C composite material of porous, in porous carbon-silicon composite material silicone content be 20%-60%, carbon Content is 40%-80%, and tap density is 0.6-0.9g/cm3
5) in step 4) obtained by Si-C composite material hole in, fill inorganic or organic carbon source, configuration viscosity it is higher Concentrated solution, carry out spray drying treatment, obtain the spherical composite of densification, and be sintered under non-oxidizing atmosphere, The Silicon-carbon composite material for lithium ion battery of high-tap density, stable circulation is finally given, silicone content is in composite 10%-40%, carbon content are 60%-90%, and tap density is 0.7-1.1g/cm3
Wherein step 1) described in the particle diameter of silica flour be 50nm-20 μm, the particle diameter of the silica flour after milled processed is 30nm- 500nm;The high molecular polymer is at least one in following substances:Phenolic resin, pitch, polyvinylidene fluoride (PVDF), polyvinylpyrrolidone (PVP), polyvinyl alcohol (PVA), polyethylene glycol oxide (PEO), polyvinyl chloride (PVC), polypropylene Nitrile (PAN), polyacetylene, glucose, sucrose, citric acid, sodium alginate, carboxymethylcellulose calcium, hydroxypropyl cellulose, poly- second two Alcohol, gelatin, starch, shitosan, alginic acid;At least one of the source of aluminium for following substances:It is aluminium isopropoxide, three aluminium ethylates, secondary Aluminium butoxide, aluminum acetate, preferably aluminium isopropoxide.
Wherein step 2) described in the condition of rotary evaporation be:Temperature is 30 DEG C -70 DEG C, and preferably 60 DEG C, rotary speed is 30-150 rev/min, preferably 120 revs/min;The thickness of amorphous carbon or alundum (Al2O3) is preferably 10-20nm, and content is excellent Elect 1%-5% as.
Step 2), 4) and 5) described in non-oxidizing atmosphere provided by following at least one gases:Nitrogen, argon gas, helium, The sintering temperature be 500-1100 DEG C, preferably 700-1000 DEG C, programming rate be 1-15 DEG C/min, preferably 1-5 DEG C/ Min, sintering time are 1-15h, preferably 2-6h.
Step 3) described in inorganic carbon source be selected from following at least one:Soft carbon, hard carbon, Scaly graphite, aphanitic graphite, people Make graphite, electrically conductive graphite, MCMB, Graphene, CNT;The polymeric additive be following substances in extremely Few one kind:It is phenolic resin, pitch, polyvinylidene fluoride (PVDF), polyvinylpyrrolidone (PVP), polyvinyl alcohol (PVA), poly- Ethylene oxide (PEO), polyvinyl chloride (PVC), polyacrylonitrile (PAN), polyacetylene, polyaniline, polythiophene;The hydroxy compounds At least one of the dispersant for following substances:Glucose, sucrose, citric acid, sodium alginate, carboxymethylcellulose calcium, hydroxypropyl are fine Dimension element, gelatin, starch, shitosan, alginic acid;The viscosity is to test under 293K in temperature, and viscosity can be 1-104MPa s, Preferably 100-500mPa s.
Step 3) in silica flour can be (1-8) with the mass ratio of inorganic carbon source:(2-9), preferably (2-7):(3-8), specifically Can be 2:8、3:7、4:6、5:5、6:4、7:3、8:2;In the solution, silica flour can be 1- with the mass concentration sum of inorganic carbon source 50%.The additives ratio is silica flour and the 0.1-30% of inorganic carbon source gross mass, preferably 1%-10%, the dispersion Agent ratio is the 0.1-60%, preferably 20%-40% of silica flour and carbon source gross mass.
Step 4) and 5) described in be spray-dried air inlet temperature can be 120-220 DEG C, preferably 160-220 DEG C, discharging Mouth temperature is 60 DEG C -120 DEG C, preferably 60-100 DEG C.The spray drying device feed pump frequency can be 10-50Hz.
Step 5) described in inorganic or organic carbon source be the high carbon source of phosphorus content or graphitized carbon, selected from it is following at least It is a kind of:Delanium, electrically conductive graphite, MCMB, Graphene, carbon nanometer, coal tar, asphalt, phenolic resin, sea Mosanom, carboxymethylcellulose calcium, hydroxypropyl cellulose, gelatin, polyvinylpyrrolidone (PVP);The viscosity in temperature is Test under 293K, viscosity can be 100-106MPa s, preferably 300-800mPa s.
The particle diameter of Si-C composite material provided by the present invention is 1-20 μm;The silica flour of uniform cladding is uniformly dispersed in material The inside of material;By way of being repeatedly spray-dried, fine and close spherical Si-C composite material is formed;Solved by multi-buffering-layer Defect of the silicon class material in lithium battery applications.
Another object of the present invention is to provide the application of the Si-C composite material.
Application provided by the present invention is application of the silicon carbide composite particles as battery electrode material, especially as lithium from The application of sub- cell negative electrode material.
Compared with prior art, the present invention is provided preparation method low cost, degree of being practical is high, can prepare on a large scale, Capacity controllable, excellent performance, and the Si-C composite material for obtaining is integrated with the advantage of Si-C composite material and porous material, passes through Multi-buffering-layer, improve silica-base material as cyclicity that lithium ion battery negative material is present it is poor, coulombic efficiency is low asks Topic, and we can also prepare reversible capacity in 400- by the ratio of silica flour and carbon source in regulation and control experimentation Composite between 1200mAh/g.
Description of the drawings
Electron scanning micrographs of the Fig. 1 for 1 gained Sample Spray dry of embodiment.
Fig. 2 is the electron scanning micrograph that embodiment 1 obtains Sample Spray dry after carbon source filling.
Fig. 3 be the Si-C composite material obtained with embodiment 1 as negative material, under the conditions of 100mA/g constant current charge-discharges First circle charging and discharging curve.
Fig. 4 be the Si-C composite material obtained with embodiment 2 as negative material, under the conditions of 100mA/g constant current charge-discharges First circle charging and discharging curve.
Fig. 5 is the electron scanning micrograph of the fine and close Si-C composite material product obtained with embodiment 8.
Specific embodiment
With reference to specific embodiment, the invention will be further described, but the present invention is not limited to following examples.
Experimental technique described in following embodiments, if no special instructions, is conventional method;The reagent and material, such as Without specified otherwise, commercially obtain.
The preparation of embodiment 1, Si-C composite material and its electrochemical property test:
By business silica flour with after ball mill pretreatment, addition sand mill carries out sand milling, the silica flour of the size needed for obtaining.Press Silica flour:Glucose=10:Silica flour, with water as solvent, is dispersed in the aqueous solution containing glucose by ultrasonically treated by 1 ratio In, the solution for obtaining is reduced pressure at 60 DEG C rotary evaporation, after by sample at 600 DEG C of blanket of nitrogen sintering processes, obtain without fixed The silica flour of shape carbon coating.
By silica flour:Graphite=7:3 mass ratio mixing, with water as solvent, PVP is additive, and sucrose is dispersant, in room Lower stirring more than the 5h of temperature, obtains the slurry that viscosity is 100mPa s.Slurry is spray-dried, inlet temperature is 180 DEG C, discharging opening temperature be 100 DEG C, after by Sample Spray dry 600 DEG C sinter, obtain the Si-C composite material of porous, porous In carbon-silicon composite material, silicone content is 65%, and carbon content is 35%, and tap density is 0.63g/cm3
Sample after sintering is mixed with electrically conductive graphite, carboxymethylcellulose calcium, more than 10h is stirred, obtaining viscosity is The slurry of 400mPa s, slurry is spray-dried, inlet temperature be 200 DEG C, discharging opening temperature be 90 DEG C, after will spray Mist drying sample is sintered for 1000 DEG C in a nitrogen atmosphere, obtains the Si-C composite material of densification, and carbon content is 55%, and silicone content is 45%, tap density is 0.76g/cm3
The sign of silicon carbide composite particles:
The particle diameter of the Si-C composite material obtained under above-mentioned condition is detected with NEC's ESEM (JEOL-6700F) And size distribution, as a result show the size distribution of Si-C composite material than more uniform, particle diameter between 1-20 μm (see Fig. 2).
The Electrochemical Characterization of silicon carbide composite particles:
By the Si-C composite material prepared in embodiment 1, acetylene black and Kynoar (binding agent) with mass ratio 80:10:10 mixing are made into slurry, are homogeneously applied to obtain cathode membrane in copper foil current collector.Using metal lithium sheet as positive pole, Microporous polypropylene membrane (Celgard 2400) is used as barrier film, 1mol/L LiPF6(it is 1 that solvent is volume ratio:1 ethylene carbonate With dimethyl carbonate mixed liquor) as electrolyte, button cell is assembled in the glove box of argon gas protection, carries out charge and discharge electrical measurement Examination, test program is 100mA/g, and it is 0.01~1.0V that charging/discharging voltage is interval, and first circle charging and discharging curve is shown in Fig. 3.Battery testing As a result it is listed in table 1.
First charge-discharge cycle efficieny is more than 80%, and initial charge capacity is 880mAh/g, circulates 50 charging specific volumes afterwards Measure as 723mAh/g.
Embodiment 2:
By business silica flour with after ball mill pretreatment, addition sand mill carries out sand milling, the silica flour of the size needed for obtaining.Press Silica flour:Citric acid=10:1 ratio, with water as solvent, is dispersed in silica flour containing lemon aqueous acid by ultrasonically treated In, the solution for obtaining is reduced pressure at 60 DEG C rotary evaporation, after by sample at 600 DEG C of argon atmospher sintering processes, obtain carbon bag The silica flour for covering.
By silica flour:Graphite=6:4 mass ratio mixing, with water as solvent, PVP is additive, and sucrose is dispersant, in room Lower stirring more than the 5h of temperature, obtains the slurry that viscosity is 100mPa s.Slurry is spray-dried, inlet temperature is 180 DEG C, discharging opening temperature is 100 DEG C, after by Sample Spray dry in 600 DEG C of argon atmospher sintering, obtain the silicon-carbon composite wood of porous Material, in porous carbon-silicon composite material, silicone content is 54%, and carbon content is 46%, and tap density is 0.74g/cm3
Sample after sintering is mixed with electrically conductive graphite, carboxymethylcellulose calcium, more than 10h is stirred, obtaining viscosity is The slurry of 400mPa s, slurry is spray-dried, inlet temperature be 200 DEG C, discharging opening temperature be 90 DEG C, after will spray Mist drying sample obtains the Si-C composite material of densification in 1000 DEG C of sintering of argon atmospher, and in carbon-silicon composite material, silicone content is 34%, carbon content is 66%, and tap density is 0.8g/cm3
The positive pole of battery, negative pole, electrolyte and battery assemble same as Example 1, the composition of gained silicon carbide composite particles And table 1 is listed in the test result of simulated battery, first circle charging and discharging curve is shown in Fig. 4.
Embodiment 3:
By business silica flour with after ball mill pretreatment, addition sand mill carries out sand milling, the silica flour of the size needed for obtaining.Press Silica flour:Sucrose=10:1 ratio, with water as solvent, is dispersed in silica flour in the aqueous solution containing sucrose by ultrasonically treated, The solution for obtaining is reduced pressure at 60 DEG C rotary evaporation, after by sample at 600 DEG C of blanket of nitrogen sintering processes, obtain carbon coating Silica flour.
By silica flour:Graphite=5:5 mass ratio mixing, with water as solvent, starch is additive, and sucrose is dispersant, More than 5h is stirred under room temperature, obtains the slurry that viscosity is 100mPa s.Slurry is spray-dried, inlet temperature is 180 DEG C, discharging opening temperature is 100 DEG C, after by Sample Spray dry in 600 DEG C of blanket of nitrogen sintering, obtain the silicon-carbon composite wood of porous Material, in porous carbon-silicon composite material, silicone content is 44%, and carbon content is 56%, and tap density is 0.76g/cm3
Sample after sintering is mixed with electrically conductive graphite, carboxymethylcellulose calcium, more than 10h is stirred, obtaining viscosity is The slurry of 400mPa s, slurry is spray-dried, inlet temperature be 200 DEG C, discharging opening temperature be 90 DEG C, after will spray Mist drying sample obtains the Si-C composite material of densification in 1000 DEG C of sintering of blanket of nitrogen, and in carbon-silicon composite material, silicone content is 24%, carbon content is 76%, and tap density is 0.83g/cm3
The positive pole of battery, negative pole, electrolyte and battery assemble same as Example 1, the composition of gained silicon carbide composite particles And table 1 is listed in the test result of simulated battery.
Embodiment 4:
By business silica flour with after ball mill pretreatment, addition sand mill carries out sand milling, the silica flour of the size needed for obtaining.Press Silica flour:PVP=10:1 ratio, with water as solvent, is dispersed in silica flour in the aqueous solution containing PVP by ultrasonically treated, will The solution for obtaining reduces pressure at 60 DEG C rotary evaporation, after by sample at 600 DEG C of argon atmospher sintering processes, obtain the silicon of carbon coating Powder.
By silica flour:Graphite=4:6 mass ratio mixing, with water as solvent, gelatin is additive, 5h is stirred at room temperature with On, obtain the slurry that viscosity is 100mPa s.Slurry is spray-dried, inlet temperature is 180 DEG C, discharging opening temperature For 100 DEG C, after by Sample Spray dry in 600 DEG C of argon atmospher sintering, obtain the Si-C composite material of porous, porous carbon silicon is combined In material, silicone content is 35%, and carbon content is 65%, and tap density is 0.74g/cm3
Sample after sintering is mixed with electrically conductive graphite, carboxymethylcellulose calcium, more than 10h is stirred, obtaining viscosity is The slurry of 400mPa s, slurry is spray-dried, inlet temperature be 200 DEG C, discharging opening temperature be 90 DEG C, after will spray Mist drying sample obtains the Si-C composite material of densification in 1000 DEG C of sintering of argon atmospher, and in carbon-silicon composite material, silicone content is 18%, carbon content is 82%, and tap density is 0.85g/cm3
The positive pole of battery, negative pole, electrolyte and battery assemble same as Example 1, the composition of gained silicon carbide composite particles And table 1 is listed in the test result of simulated battery.
Embodiment 5:
By business silica flour with after ball mill pretreatment, addition sand mill carries out sand milling, the silica flour of the size needed for obtaining.Press Silica flour:Aluminium isopropoxide=10:1 ratio, with isopropanol as solvent, is dispersed in silica flour containing aluminium isopropoxide by ultrasonically treated Aqueous isopropanol in, the solution for obtaining is reduced pressure at 60 DEG C rotary evaporation, after by sample at 600 DEG C of helium-atmosphere at sintering Reason, obtains the silica flour of alundum (Al2O3) cladding.
By silica flour:Graphite=6:4 mass ratio mixing, with water as solvent, polyacrylonitrile is additive, and sucrose is dispersion Agent, is stirred at room temperature more than 5h, obtains the slurry that viscosity is 100mPa s.Slurry is spray-dried, inlet temperature For 180 DEG C, discharging opening temperature is 100 DEG C, after by Sample Spray dry in 600 DEG C of sintering of helium-atmosphere, the silicon-carbon for obtaining porous is multiple Condensation material, in porous carbon-silicon composite material, silicone content is 54%, and carbon content is 46%, and tap density is 0.71g/cm3
Sample after sintering is mixed with electrically conductive graphite, carboxymethylcellulose calcium, more than 10h is stirred, obtaining viscosity is The slurry of 400mPa s, slurry is spray-dried, inlet temperature be 200 DEG C, discharging opening temperature be 90 DEG C, after will spray Mist drying sample obtains the Si-C composite material of densification in 1000 DEG C of sintering of helium-atmosphere, and in carbon-silicon composite material, silicone content is 34%, carbon content is 66%, and tap density is 0.81g/cm3
The positive pole of battery, negative pole, electrolyte and battery assemble same as Example 1, the composition of gained silicon carbide composite particles And table 1 is listed in the test result of simulated battery.
Embodiment 6:
By business silica flour with after ball mill pretreatment, addition sand mill carries out sand milling, the silica flour of the size needed for obtaining.Silicon Powder:Three aluminium ethylate=10:Silica flour, with ethanol as solvent, is dispersed in the second containing three aluminium ethylates by ultrasonically treated by 1 ratio In alcoholic solution, the solution for obtaining is reduced pressure at 60 DEG C rotary evaporation, after by sample at 600 DEG C of argon atmospher sintering processes, obtain To the silica flour of alundum (Al2O3) cladding.
By silica flour:Graphite=6:4 mass ratio mixing, with water as solvent, PVP is additive, and the weight average molecular weight of PVP is 300000, sucrose is dispersant, and more than 5h is stirred at room temperature, and obtains the slurry that viscosity is 100mPa s.Slurry is sprayed Mist is dried, and inlet temperature is 180 DEG C, and discharging opening temperature is 100 DEG C, after by Sample Spray dry in 600 DEG C of argon atmospher sintering, The Si-C composite material of porous is obtained, silicone content is 45% in porous carbon-silicon composite material, and carbon content is 55%, and tap density is 0.74g/cm3
Sample after sintering is mixed with electrically conductive graphite, carboxymethylcellulose calcium, more than 10h is stirred, obtaining viscosity is The slurry of 400mPa s, slurry is spray-dried, inlet temperature be 200 DEG C, discharging opening temperature be 90 DEG C, after will spray Mist drying sample obtains the Si-C composite material of densification in 1000 DEG C of sintering of argon atmospher, and in carbon-silicon composite material, silicone content is 33%, carbon content is 67%, and tap density is 0.86g/cm3
The positive pole of battery, negative pole, electrolyte and battery assemble same as Example 1, the composition of gained silicon carbide composite particles And table 1 is listed in the test result of simulated battery.
Embodiment 7:
Other conditions are same as Example 6, and difference is silica flour:Graphite=5:5.
The silicone content of the fine and close Si-C composite material of gained is 28%, and carbon content is 72%, and tap density is 0.85g/cm3。 The composition of gained silicon carbide composite particles and table 1 is listed in the test result of simulated battery.
Embodiment 8:
By business silica flour with after ball mill pretreatment, addition sand mill carries out sand milling, the silica flour of the size needed for obtaining.Silicon Powder:Aluminium secondary butylate=10:Silica flour, with sec-butyl alcohol as solvent, is disperseed in aqueous by 1 ratio by ultrasonically treated, will To solution reduce pressure at 60 DEG C rotary evaporation, after by sample at 600 DEG C of blanket of nitrogen sintering processes, obtain alundum (Al2O3) bag The silica flour for covering.
By silica flour:Graphite=4:6 mass ratio mixing, with water as solvent, PVP is additive, and sucrose is dispersant, in room Lower stirring more than the 5h of temperature, obtains the slurry that viscosity is 100mPa s.Slurry is spray-dried, inlet temperature is 180 DEG C, discharging opening temperature is 100 DEG C, after by Sample Spray dry in 600 DEG C of blanket of nitrogen sintering, obtain the silicon-carbon composite wood of porous Material, in porous carbon-silicon composite material, silicone content is 34%, and carbon content is 66%, tap density 0.79g/cm3
Sample after sintering is mixed with Graphene, gelatin, asphalt, more than 10h is stirred, obtaining viscosity is The slurry of 400mPa s, slurry is spray-dried, inlet temperature be 200 DEG C, discharging opening temperature be 90 DEG C, after will spray Mist drying sample obtains the Si-C composite material of densification in 1000 DEG C of sintering of blanket of nitrogen, and in composite, silicone content is 22%, carbon Content is 78%, and tap density is 0.9g/cm3
The positive pole of battery, negative pole, electrolyte and battery assemble same as Example 1, the composition of gained silicon carbide composite particles And table 1 is listed in the test result of simulated battery, stereoscan photograph such as Fig. 5 of gained densification Si-C composite material.
Embodiment 9:
By business silica flour with after ball mill pretreatment, addition sand mill carries out sand milling, the silica flour of the size needed for obtaining.Silicon Powder:Aluminum acetate=10:1 ratio, dissolves aluminum acetate by solvent of water, alumine hydroxide colloid is obtained, leads to after being sufficiently stirred for hydrolysis Cross ultrasonically treated by silica flour dispersed gained alumine hydroxide colloid, the solution for obtaining reduced pressure at 60 DEG C rotary evaporation, Afterwards by sample at 600 DEG C of argon atmospher sintering processes, obtain the silica flour of alundum (Al2O3) cladding.
By silica flour:Graphite=4:6 mass ratio mixing, with water as solvent, sodium alginate is additive, and citric acid is dispersion Agent, is stirred at room temperature more than 5h, obtains the slurry that viscosity is 100mPa s.Slurry is spray-dried, inlet temperature For 180 DEG C, discharging opening temperature is 100 DEG C, after by Sample Spray dry in 600 DEG C of sintering of argon atmospher, the silicon-carbon for obtaining porous is multiple Condensation material, in porous carbon-silicon composite material, silicone content is 35%, and carbon content is 65%, and tap density is 0.77g/cm3
Sample after sintering is mixed with asphalt, carboxymethylcellulose calcium, more than 10h is stirred, obtaining viscosity is The slurry of 400mPa s, slurry is spray-dried, inlet temperature be 200 DEG C, discharging opening temperature be 90 DEG C, after will spray Mist drying sample obtains the Si-C composite material of densification in 1000 DEG C of sintering of argon atmospher, and in composite, silicone content is 19%, carbon Content is 81%, and tap density is 0.88g/cm3
The positive pole of battery, negative pole, electrolyte and battery assemble same as Example 1, the composition of gained silicon carbide composite particles And table 1 is listed in the test result of simulated battery.
Comparative example 1:
By silica flour:Graphite=4:6 mass ratio mixing, with water as solvent, PVP is additive, and sucrose is dispersant, in room Lower stirring more than the 5h of temperature, obtains the slurry that viscosity is 100mPa s.Slurry is spray-dried, inlet temperature is 180 DEG C, discharging opening temperature be 100 DEG C, after by Sample Spray dry 1000 DEG C sinter, the Si-C composite material tap density for obtaining For 0.5g/cm3.The positive pole of battery, negative pole, electrolyte and battery assemble same as Example 1, the group of gained silicon carbide composite particles Into and be listed in table 1 in the test result of simulated battery.
Comparative example 2:
By silica flour:Glucose=10:1 ratio, with water as solvent, is dispersed in silica flour containing grape by ultrasonically treated Sugar the aqueous solution in, by the solution for obtaining at 60 DEG C rotary evaporation, after by sample at 600 DEG C sintering processes, obtain carbon bag The silica flour for covering.
By silica flour:Graphite=6:4 mass ratio mixing, with water as solvent, PVP is additive, and sucrose is dispersant, in room Lower stirring more than the 5h of temperature, obtains the slurry that viscosity is 100mPa s.Slurry is spray-dried, inlet temperature is 180 DEG C, discharging opening temperature be 100 DEG C, after by Sample Spray dry 1000 DEG C sinter, the Si-C composite material tap density for obtaining For 0.53g/cm3
The positive pole of battery, negative pole, electrolyte and battery assemble same as Example 1, the composition of gained silicon carbide composite particles And table 1 is listed in the test result of simulated battery.
Comparative example 3:
By silica flour:Graphite=4:6 mass ratio mixing, with water as solvent, PVP is additive, and sucrose is dispersant, in room Lower stirring more than the 5h of temperature, obtains the slurry that viscosity is 100mPa s.Slurry is spray-dried, inlet temperature is 180 DEG C, discharging opening temperature be 100 DEG C, after by Sample Spray dry 600 DEG C sinter.
Sample after sintering is mixed with electrically conductive graphite, more than 10h is stirred, the slurry that viscosity is 400mPa s is obtained, will Slurry is spray-dried, inlet temperature be 200 DEG C, discharging opening temperature be 90 DEG C, after by Sample Spray dry at 1000 DEG C Sintering, obtains the Si-C composite material of densification, and tap density is 0.75g/cm3
The positive pole of battery, negative pole, electrolyte and battery assemble same as Example 1, the composition of gained silicon carbide composite particles And table 1 is listed in the test result of simulated battery.
The composition of table 1, Si-C composite material and under the conditions of 100mA/g constant current charge-discharge test result

Claims (10)

1. a kind of preparation method of Silicon-carbon composite material for lithium ion battery, comprises the following steps that:
1) by sanded treatment after silica flour ball mill grinding, the silica flour after process is dispersed in into the solution containing silicon source or containing silicon source It is in colloid and ultrasonically treated, make silica flour suspend in the solution, prevent to reunite;
2) by step 1) obtained by solution decompression rotary evaporation remove solvent after, be sintered under non-oxidizing atmosphere, in silicon Surface coating alundum (Al2O3), the thickness of alundum (Al2O3) is 5 30nm, and content is 0.5% 10%;
3) by step 2) obtained by the silica flour that coats be 50000 with inorganic carbon source, hydroxy compounds dispersant, weight average molecular weight 400000 polymeric additive carries out mechanical agitation, is uniformly mixed, the suitable weak solution of viscosity;
4) by step 3) obtained by weak solution carry out spray drying treatment, obtain Si-C composite material, and in non-oxidizing atmosphere Under be sintered, obtain the Si-C composite material of porous, in porous carbon-silicon composite material, silicone content is 20% 60%, carbon content For 40% 80%, tap density is 0.6 0.9g/cm3
5) in step 4) obtained by Si-C composite material hole in, fill inorganic or organic carbon source, configure higher dense of viscosity Solution, carries out spray drying treatment, obtains the spherical composite of densification, and is sintered under non-oxidizing atmosphere, finally Silicon-carbon composite material for lithium ion battery is obtained, silicone content is 10% 40% in composite, carbon content is 60% 90%, is shaken Real density is 0.7 1.1g/cm3
2. method according to claim 1, it is characterised in that:Step 1) described in silica flour particle diameter be 20 μm of 50nm, grind The particle diameter of the silica flour after mill process is 30nm 500nm;At least one of the source of aluminium selected from following substances:Aluminium isopropoxide, three second Aluminium alcoholates, aluminium secondary butylate, aluminum acetate, Tributyl aluminate.
3. the method according to one of claim 12, it is characterised in that:Wherein step 2) described in rotary evaporation condition For:Temperature is 30 DEG C 70 DEG C, and rotary speed is 30 150 revs/min;The thickness of alundum (Al2O3) is 10 20nm, and content is 1% 5%.
4. the method according to one of claim 12, it is characterised in that:Step 2), 4) and 5) described in non-oxidizing gas Atmosphere is provided by following at least one gases:Nitrogen, argon gas, helium, the sintering temperature are 500 1100 DEG C, and programming rate is 1 15 DEG C/min, sintering time is 1 15h.
5. the method according to one of claim 12, it is characterised in that:Step 3) described in inorganic or organic carbon source be selected from Following at least one:Soft carbon, hard carbon, Scaly graphite, aphanitic graphite, Delanium, electrically conductive graphite, MCMB, stone Black alkene, CNT;The additive is at least one in following substances:It is phenolic resin, pitch, polyvinylidene fluoride, poly- Vinylpyrrolidone, polyvinyl alcohol, polyethylene glycol oxide, polyvinyl chloride, polyacrylonitrile, polyacetylene, polyaniline, polythiophene;It is described At least one of the dispersant for following substances:Glucose, sucrose, citric acid, sodium alginate, carboxymethylcellulose calcium, hydroxypropyl are fine Dimension element, polyethylene glycol, gelatin, starch, shitosan, alginic acid;The viscosity is to test under 293K in temperature, and viscosity can be 1 104mPa·s。
6. the method according to one of claim 12, it is characterised in that:Step 4) and 5) described in be spray-dried air inlet Temperature is 120 220 DEG C, and discharging opening temperature is 60 DEG C 120 DEG C, and the spray drying device feed pump frequency is 10 30Hz.
7. the method according to one of claim 12, it is characterised in that:Step 5) described in carbon source be selected from following It is at least one:Delanium, electrically conductive graphite, MCMB, Graphene, carbon nanometer, coal tar, asphalt, phenolic aldehyde tree Fat, sodium alginate, carboxymethylcellulose calcium, hydroxypropyl cellulose, gelatin, polyvinylpyrrolidone;The viscosity in temperature is Test under 293K, viscosity can be 100 106mPa·s。
8. the method according to one of claim 12, it is characterised in that:Step 5) described in carbon source contain gelatin simultaneously And Graphene.
9. the Si-C composite material that arbitrary methods described is prepared in claim 18.
10. application of the Si-C composite material described in claim 9 as lithium ion battery negative material.
CN201510106478.7A 2015-03-11 2015-03-11 Silicon-carbon composite material for lithium ion battery, preparation method and application of silicon-carbon composite material Active CN104716312B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510106478.7A CN104716312B (en) 2015-03-11 2015-03-11 Silicon-carbon composite material for lithium ion battery, preparation method and application of silicon-carbon composite material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510106478.7A CN104716312B (en) 2015-03-11 2015-03-11 Silicon-carbon composite material for lithium ion battery, preparation method and application of silicon-carbon composite material

Publications (2)

Publication Number Publication Date
CN104716312A CN104716312A (en) 2015-06-17
CN104716312B true CN104716312B (en) 2017-03-22

Family

ID=53415433

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510106478.7A Active CN104716312B (en) 2015-03-11 2015-03-11 Silicon-carbon composite material for lithium ion battery, preparation method and application of silicon-carbon composite material

Country Status (1)

Country Link
CN (1) CN104716312B (en)

Families Citing this family (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3133690A1 (en) * 2015-07-20 2017-02-22 Commissariat A L'energie Atomique Et Aux Energies Alternatives Silicon-carbon composite particulate material
CN105552357B (en) * 2016-01-29 2018-10-02 银隆新能源股份有限公司 Lithium titanate electrode material and preparation method thereof
CN105702924B (en) * 2016-01-29 2018-10-02 银隆新能源股份有限公司 Lithium titanate electrode material and preparation method thereof
DE102016203352A1 (en) * 2016-03-01 2017-09-07 Wacker Chemie Ag Process for processing electrode materials for batteries
CN105742599B (en) * 2016-03-18 2019-04-26 苏州协鑫集成科技工业应用研究院有限公司 Si-C composite material and preparation method thereof and negative electrode material and battery
CN107293700B (en) * 2016-03-31 2020-08-07 比亚迪股份有限公司 Lithium ion battery negative electrode active material, preparation method thereof, negative electrode and battery
CN105655570B (en) * 2016-04-01 2018-08-21 四川创能新能源材料有限公司 A kind of method prepared by the fining of nano silicone powder material
CN106920938A (en) * 2017-03-30 2017-07-04 天津中科先进技术研究院有限公司 Silicon-carbon composite material and preparation method thereof
CN110197895A (en) * 2018-02-26 2019-09-03 华为技术有限公司 A kind of composite material and preparation method
CN108987693B (en) * 2018-07-09 2021-10-22 浙江工业职业技术学院 Preparation method of high-performance carbon-silicon composite material for lithium battery
CN108987692B (en) * 2018-07-09 2021-10-22 浙江工业职业技术学院 Preparation method of carbon-silicon composite material with mesoporous structure
CN109004188B (en) * 2018-07-09 2022-03-25 绍兴文理学院 Green preparation method of porous carbon-silicon composite material
CN109935832B (en) * 2018-11-21 2020-12-15 万向一二三股份公司 Silicon-based negative electrode binder of lithium ion battery and preparation method of negative plate using binder
CN109755509A (en) * 2018-12-21 2019-05-14 江苏大学 A kind of lithium ion battery Si@Nb2O5The preparation method of composite negative pole material
CN109817966B (en) * 2019-01-07 2022-01-04 宁波维科电池有限公司 Preparation method of lithium ion battery cathode composite material
CN114975980A (en) * 2019-03-19 2022-08-30 宁德新能源科技有限公司 Negative electrode material, and electrochemical device and electronic device using same
CN110165178B (en) * 2019-05-24 2022-07-08 东莞市安德丰电池有限公司 Lithium battery positive electrode material, preparation method thereof and lithium battery containing positive electrode material
CN110518224A (en) * 2019-09-09 2019-11-29 厦门大学 A kind of preparation method of lithium ion battery carbon silicon anode material
CN110790573B (en) * 2019-11-25 2021-01-15 北京科技大学 Method for thoroughly eliminating lithium carbonate by garnet type lithium ion solid electrolyte
CN111063875A (en) * 2019-12-25 2020-04-24 广东凯金新能源科技股份有限公司 Spongy porous structure silicon-based composite material and preparation method thereof
CN111653739B (en) * 2020-04-28 2021-05-18 万向一二三股份公司 Method for preparing high-cycle-performance SiO negative electrode material of lithium battery
CN111977658B (en) * 2020-08-26 2021-03-02 成都新柯力化工科技有限公司 Method for continuously producing silicon-carbon negative electrode material of lithium battery
CN113659125B (en) * 2021-07-02 2022-07-12 广东墨睿科技有限公司 Silicon-carbon composite material and preparation method thereof
CN116253311A (en) * 2023-02-24 2023-06-13 四川兴储能源科技有限公司 Preparation and application of three-dimensional porous hard carbon material

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101153358A (en) * 2006-09-28 2008-04-02 深圳市比克电池有限公司 Method of producing silicon carbon negative pole material of lithium ion battery
CN101859886A (en) * 2010-05-27 2010-10-13 深圳市德兴富电池材料有限公司 Lithium ion battery anode material and preparation method thereof
CN101850959B (en) * 2010-05-31 2012-03-28 奇瑞汽车股份有限公司 Method for preparing silicon-carbon cathode material of lithium ion battery
CN102637872A (en) * 2012-01-07 2012-08-15 天津市贝特瑞新能源材料有限责任公司 High-capacity silicon-carbon composited anode material, preparation method and application thereof
CN102694155B (en) * 2012-05-31 2014-11-26 奇瑞汽车股份有限公司 Silicon-carbon composite material, preparation method thereof and lithium ion battery employing same
CN103236525B (en) * 2013-05-06 2015-09-23 奇瑞汽车股份有限公司 A kind of Si-C composite material and preparation method thereof, lithium ion battery
CN103311523B (en) * 2013-06-04 2017-02-08 清华大学深圳研究生院 Silicon-carbon composite material with nano micropores and preparation method as well as application thereof

Also Published As

Publication number Publication date
CN104716312A (en) 2015-06-17

Similar Documents

Publication Publication Date Title
CN104716312B (en) Silicon-carbon composite material for lithium ion battery, preparation method and application of silicon-carbon composite material
CN104868107B (en) A kind of lithium ion battery spherical Si-C composite material and its preparation method and application
CN107369823B (en) Artificial graphite composite negative electrode material for lithium ion battery and preparation method thereof
CN102694155B (en) Silicon-carbon composite material, preparation method thereof and lithium ion battery employing same
CN106099061B (en) A kind of porous graphene/silicon composite, preparation method and lithium ion battery
CN105932245B (en) A kind of high compacted density silicon-carbon cathode material and its preparation method and application
CN108630920A (en) A kind of nano-metal-oxide/MXene heterojunction structure composite material and preparation methods
CN106587055A (en) Biomass-based porous carbon material, preparation method thereof, and application thereof in supercapacitor
CN104986758A (en) Three-dimensional network graphene for lithium battery and preparing method thereof
CN108123111A (en) A kind of lithium ion battery silicon substrate composite negative pole material, its preparation method and the negative electrode of lithium ion battery comprising the material
Liu et al. Biomass-derived Activated Carbon for Rechargeable Lithium-Sulfur Batteries.
CN106410177B (en) A kind of elliposoidal SiOx/ graphite cathode composite materials and its preparation method and application
CN105264654A (en) Combined electrochemical and chemical etching processes for generation of porous silicon particulates
CN105047427B (en) Ultracapacitor combination electrode material and preparation method thereof and ultracapacitor
CN103346325A (en) Lithium ion battery cathode material and preparation method thereof as well as lithium ion battery
CN108448080A (en) A kind of graphene coated silicon/metal composite negative pole material and preparation method thereof
CN101944596A (en) Preparation method of silicon and carbon composite microspheres and application thereof
CN108598391A (en) A kind of nano silicon composite cathode material for lithium ion battery
CN109360962B (en) High-stability silicon-carbon negative electrode material for lithium battery and preparation method thereof
CN111063872A (en) Silicon-carbon negative electrode material and preparation method thereof
CN107887602A (en) A kind of classifying porous charcoal nanometer sheet electrode material of nitrogen oxygen codope and its preparation method and application
CN110707323B (en) Anion layer-expanding carbon material and preparation method and application thereof
CN106450315B (en) A kind of high performance carbon paper base electrode anode material and its preparation method and application
CN100383037C (en) Carbon material and nano silicon composite materials and method for preparing same and use thereof
CN103022435A (en) Lithium ion battery silicon-carbon composite negative electrode material and preparation method thereof

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20180315

Address after: 100080 Beijing city Haidian District xicaochang No. 5 floor No. 85459

Patentee after: Beijing one gold Amperex Technology Limited

Address before: 100190 Haidian District, Zhongguancun, North Street, No. 1, No. 2, Beijing

Patentee before: Institute of Chemistry, Chinese Academy of Sciences

TR01 Transfer of patent right