The content of the invention
In view of the shortcomings of the prior art, it is an object of the invention to invent a kind of high power capacity carbon-silicon composite material, its system
Preparation Method and the lithium ion battery comprising the carbon-silicon composite material, carbon-silicon composite material Stability Analysis of Structures of the invention, nano-silicon
Good dispersion and nano-silicon are wrapped by that degree is very high, as the negative material of lithium ion battery, show de- lithium ratio very high
Capacity, good cycle and fills excellent soon, takes off lithium specific capacity in more than 391.7mAh/g, 50 appearances of 1.0C constant current charge-discharges
More than 95.3%, 10min charge rates are up to 90.2% for amount conservation rate.
It is that, up to above-mentioned purpose, the present invention is adopted the following technical scheme that:
In a first aspect, the present invention provides a kind of carbon-silicon composite material, the carbon-silicon composite material includes kernel and cladding
In the shell of core surface, wherein, the kernel is amorphous carbon, the shell be scattered in pyrolytic carbon layer by nano-silicon and
Formed.
Preferably, the median particle diameter of the carbon-silicon composite material is 5 μm~60 μm, for example, can be 5 μm, 7 μm, 8 μm, 10 μ
m、12μm、15μm、17μm、19μm、22μm、24μm、25μm、26μm、28μm、30μm、33μm、35μm、38μm、40μm、45μm、
48 μm, 52 μm, 56 μm or 60 μm etc., preferably 8 μm~30 μm, more preferably 10 μm~25 μm.
Preferably, the specific surface area of the carbon-silicon composite material is 0.8m2/ g~3.5m2/ g, for example, can be 0.8m2/g、
1m2/g、1.2m2/g、1.4m2/g、1.6m2/g、1.8m2/g、2m2/g、2.3m2/g、2.6m2/g、3m2/g、3.2m2/ g or 3.5m2/
G etc., preferably 1.1m2/ g~2.0m2/g。
Preferably, the compacted density of the carbon-silicon composite material is 0.9g/cm3~2.0g/cm3, for example, can be 0.9g/
cm3、1.1g/cm3、1.3g/cm3、1.5g/cm3、1.6g/cm3、1.7g/cm3、1.8g/cm3Or 2g/cm3Deng being for example preferably
1.0g/cm3~1.4g/cm3。
Preferably, the amorphous carbon includes soft carbon and/or hard carbon.
" soft carbon and/or hard carbon " of the present invention refers to:Can be soft carbon, or hard carbon, can also be soft carbon and hard
The mixture of carbon.
In the present invention, the kernel is amorphous carbon, the median particle diameter of the amorphous carbon be preferably 5 μm~30 μm, example
It such as can be 5 μm, 6 μm, 7 μm, 9 μm, 11 μm, 12 μm, 13 μm, 14 μm, 15 μm, 17 μm, 20 μm, 22 μm, 25 μm, 28 μm or 30 μm
Deng preferably 7~20 μm, more preferably 9 μm~15 μm;
Preferably, the median particle diameter of the nano-silicon be 25nm~300nm, for example can for 25nm, 35nm, 45nm, 50nm,
60nm、75nm、80nm、90nm、100nm、110nm、125nm、135nm、140nm、150nm、160nm、175nm、190nm、
210nm, 230nm, 245nm, 260nm, 280nm or 300nm etc., preferably 80nm~200nm.
Preferably, the thickness of the shell is 0~3.0 μm, and does not include 0.
Preferably, the pyrolytic carbon layer is that the binding agent is preferably wrapped as obtained from binding agent and carbon source by pyrolysis
Include in pitch, polyvinyl alcohol or phenolic resin any one or at least two mixture, but be not limited to above-mentioned enumerating
Adhesive, pyrolytic carbon can be converted into carbonisation for others and the adhesive with adhesive effect can also be used for the present invention.
Preferably, the carbon source preferably includes pitch and/or macromolecular compound.
" pitch and/or macromolecular compound " of the present invention refers to:Can be pitch, or macromolecular compound,
Can also be the mixture of pitch and macromolecular compound.
The macromolecular compound can be for example polymer and carbohydrate etc., but be not limited to polymer and carbohydrate, other
The macromolecular compound of species also can be used for the present invention as carbon source.
Preferably, the macromolecular compound includes that macromolecule is epoxy resin, phenolic resin, furfural resin, ureaformaldehyde tree
In fat, polyvinyl alcohol, polyvinyl chloride, polyethylene glycol, PEO, Kynoar, acrylic resin or polyacrylonitrile
Any one or at least two mixture, but be not limited to the macromolecular compound enumerated, carbon bag commonly used in the art
Cover and can also be used for the present invention with carbon source.
Second aspect, the present invention provides the preparation method of carbon-silicon composite material as described in relation to the first aspect, methods described bag
Include following steps:
(1) surface modification is carried out to amorphous carbon using binding agent;
(2) amorphous carbon of the binding agent modification for obtaining step (1) is combined with nano-silicon, then compound to what is obtained
Product carries out the first carbonization, obtains the first carbon silicon composite precursor;
(3) the first carbon silicon composite precursor obtained to step (2) using carbon source carries out coating modification, obtains the second carbon silicon
Composite precursor, then the second carbon silicon composite precursor to obtaining carries out the second carbonization, obtains carbon-silicon composite material.
Used as the optimal technical scheme of the method for the invention, methods described is additionally included in the carbonization of step (2) first and completes
Afterwards, the step of being sieved to the first product for obtaining of carbonization, the mesh number of the screen cloth that the sieving is used is 200 mesh or 325 mesh, preferably
It is 325 mesh.
Used as the another optimal technical scheme of the method for the invention, methods described is additionally included in the carbonization of step (3) second
After the completion of, the second product for obtaining of carbonization is crushed, is sieved and the step of except magnetic.
Preferably, step (1) described amorphous carbon includes soft carbon and/or hard carbon, for example, can be soft carbon, hard carbon, or soft carbon
With the mixture of hard carbon.
Preferably, step (1) described binding agent include pitch, polyvinyl alcohol or phenolic resin in any one or at least
Two kinds of mixture, but be not limited to the above-mentioned binding agent enumerated, it is other through carbonization can be converted into pyrolytic carbon with viscous
The binding agent of knot effect can also be used for the present invention.
Binding agent in the present invention is converted into pyrolytic carbon in follow-up carbonisation, such that it is able to make nano-silicon not only receive
The cladding of the pyrolytic carbon being converted into the follow-up carbon source for adding, also receives the cladding of the pyrolytic carbon that binding agent is converted into, so as to carry
High nano-silicon is wrapped by degree.
Preferably, the median particle of step (1) described bonding agent be less than or equal to 5 μm, for example can for 5 μm, 4.5 μm, 4 μm,
3.5 μm, 3 μm, 2 μm, 1.5 μm, 1 μm, 0.8 μm or 0.5 μm etc., preferably less than equal to 2 μm.
Preferably, the method that step (1) described surface modification is used modifies any in method or liquid phase modification method for solid phase
It is a kind of.Wherein, the preparation process of the solid phase modification method is:Binding agent and amorphous carbon are placed in VC mixers, are mixed
Close, then, mixed material is added in fusion machine and is merged, obtain the amorphous carbon of binding agent modification.
The preparation process of liquid phase modification method is:Binding agent is dissolved in solvent, amorphous carbon is added, stirring is steamed
Dry solvent, obtains the amorphous carbon of binding agent modification.
Preferably, in the solid phase modification method, during mixing, the rotating speed of VC mixers is 500r/min~3000r/min, example
Such as can for 500r/min, 700r/min, 800r/min, 1000r/min, 1200r/min, 1500r/min, 1750r/min,
1850r/min、2000r/min、2200r/min、2300r/min、2400r/min、2500r/min、2600r/min、2800r/
Min or 3000r/min etc..
Preferably, in the solid phase modification method, the time of the mixing (or breaing up) is no less than 15min, for example, can be
15min、25min、30min、40min、50min、1h、1.2h、1.5h、1.8h、2h、2.4h、2.7h、3h、4h、6h、8h、10h、
12h or 15h etc., preferably 30min;
Preferably, in the solid phase modification method, during fusion, the rotating speed for merging machine is 500r/min~3000r/min, for example
Can be 500r/min, 600r/min, 900r/min, 1000r/min, 1200r/min, 1400r/min, 1600r/min, 1800r/
Min, 2000r/min, 2200r/min, 2300r/min, 2400r/min, 2500r/min, 2600r/min, 2750r/min or
3000r/min etc.;Cutter gap width in fusion machine is preferably 0.01cm~0.5cm, for example can for 0.01cm, 0.03cm,
0.05cm, 0.1cm, 0.15cm, 0.2cm, 0.3cm, 0.35cm, 0.4cm or 0.5cm etc.;
Preferably, in the solid phase modification method, time of the fusion is no less than 0.5h, for example can for 0.5h, 1h,
1.5h, 2h, 2.4h, 3.5h, 4h, 5h, 6.5h, 7h, 8h, 9h, 10h, 12h, 15h, 20h, 24h, 28h, 30h, 32h, 34h or
36h etc., preferably 45min.
Preferably, in the liquid phase modification method, the solvent is appointing in tetrahydrofuran, toluene, carbon disulfide, alcohol or water
Meaning it is a kind of or at least two mixtures.
Preferably, step (2) the compound method is:Step (1) is obtained binding agent modification amorphous carbon and
Nano-silicon is added in solvent, stirring, solvent evaporated, is obtained so as in the presence of binding agent, make nano-silicon be bonded to step (1)
The surface of the amorphous carbon of the binding agent modification arrived, obtains combination product.
Preferably, in step (2) the compound method, the solvent is any one in isopropanol, ethanol or water
Or at least two mixture.
Preferably, step (2) it is described first carbonization carry out in an inert atmosphere, the inert atmosphere include nitrogen atmosphere,
In argon gas atmosphere, neon atmosphere, helium atmosphere, xenon atmosphere or Krypton atmosphere any one or at least two combination.
Preferably, step (2) it is described first carbonization temperature be 400 DEG C~800 DEG C, for example can for 400 DEG C, 450 DEG C,
475 DEG C, 500 DEG C, 550 DEG C, 600 DEG C, 620 DEG C, 650 DEG C, 700 DEG C, 750 DEG C or 800 DEG C etc..
Preferably, step (2) it is described first carbonization time be 2h~6h, for example can for 2h, 2.3h, 2.5h, 2.7h,
3h, 3.4h, 3.7h, 4h, 4.5h, 4.8h, 5h, 5.2h, 5.5h, 5.8h or 6h etc..
Preferably, during being warmed up to the temperature of step (2) first carbonization, heating rate is 1 DEG C/min~10
DEG C/min, for example can be 1 DEG C/min, 3 DEG C/min, 5 DEG C/min, 6 DEG C/min, 8 DEG C/min or 10 DEG C/min etc..
Preferably, step (3) described carbon source includes pitch and/or macromolecular compound, and the macromolecular compound is for example
Can be polymer and carbohydrate etc..
Preferably, the macromolecular compound includes epoxy resin, phenolic resin, furfural resin, Lauxite, polyethylene
In alcohol, polyvinyl chloride, polyethylene glycol, PEO, Kynoar, acrylic resin or polyacrylonitrile any one or
At least two mixture, but it is not limited to the macromolecular compound enumerated, carbon coating carbon source commonly used in the art
Can be used for the present invention.
Preferably, counted by 100wt% of the gross mass of carbon source and the first carbon silicon composite precursor, step (3) described carbon source
Mass percent be 5wt%~20wt%, for example can for 5wt%, 7wt%, 8wt%, 9wt%, 10wt%, 12wt%,
13wt%, 14wt%, 15wt%, 16wt%, 17wt%, 18wt% or 20wt% etc., preferably 8wt%~13wt%.
Preferably, the method that step (3) described coating modification is used is solid phase cladding process, liquid phase coating method, fusion cladding
Method or spray drying cladding process in any one.Wherein, the preparation process of the solid phase cladding process is:First carbon silicon is combined
Presoma is placed in VC mixers with carbon source, is mixed, and obtains the second carbon silicon composite precursor.
The preparation process of the liquid phase coating method is:First carbon silicon composite precursor and carbon source are added in solvent, are stirred
Mix, solvent evaporated, obtain the second carbon silicon composite precursor.
It is described fusion cladding process preparation process be:First carbon silicon composite precursor is added in the machine of fusion with carbon source
Row fusion, obtains the second carbon silicon composite precursor.
It is described spray drying cladding process preparation process be:First carbon silicon composite precursor and carbon source are added to solvent
In, stirring obtains mixed slurry, is spray-dried, and obtains the second carbon silicon composite precursor.
Preferably, in the solid phase cladding process, during mixing, the rotating speed of VC mixers is 500r/min~3000r/min, example
Such as can for 500r/min, 650r/min, 800r/min, 1000r/min, 1250r/min, 1450r/min, 1600r/min,
1900r/min, 2150r/min, 2300r/min, 2500r/min, 2700r/min or 3000r/min etc..
Preferably, in the solid phase cladding process, the time of the mixing (or breaing up) is no less than 15min, for example, can be
15min, 30min, 50min, 1h, 1.5h, 2h, 3h, 5h, 8h, 10h, 12h, 15h, 18h, 24h or 36h etc., preferably 30min;
Preferably, in the liquid phase coating method, the solvent is appointing in tetrahydrofuran, toluene, carbon disulfide, alcohol or water
Meaning it is a kind of or at least two mixtures.
Preferably, in the fusion cladding process, during fusion, the rotating speed for merging machine is 500r/min~3000r/min, for example
Can for 500r/min, 800r/min, 1000r/min, 1250r/min, 1700r/min, 2000r/min, 2300r/min,
2600r/min, 2800r/min or 3000r/min etc., the gap width of the cutter in fusion machine is 0.01cm~0.5cm, for example
Can be 0.01cm, 0.05cm, 0.1cm, 0.2cm, 0.3cm, 0.4cm or 0.5cm etc..
Preferably, in the fusion cladding process, time of the fusion is no less than 0.5h, for example can for 1h, 2h, 3h, 5h,
7h, 10h, 12h, 15h, 24h, 30h, 36h or 48h etc., preferably 45min.
Preferably, in the spray drying cladding process, the solvent is in tetrahydrofuran, toluene, carbon disulfide, alcohol or water
Any one or at least two mixture.
Preferably, in the spray drying cladding process, the condition of the spray drying is:Inlet temperature is 250 DEG C~400
DEG C, preferably 300 DEG C;Outlet temperature is 90 DEG C~115 DEG C, preferably 110 DEG C;The solid of mixed slurry for being spray-dried contains
It is 10wt%~30wt% to measure;The feed rate of mixed slurry is 10mL/min~40mL/min during spray drying.
In the spray drying cladding process, inlet temperature be 250 DEG C~400 DEG C, for example, 250 DEG C, 275 DEG C, 300 DEG C,
320 DEG C, 350 DEG C, 360 DEG C, 380 DEG C or 400 DEG C etc..
In the spray drying cladding process, outlet temperature be 90 DEG C~115 DEG C, for example, 90 DEG C, 92 DEG C, 95 DEG C, 100
DEG C, 103 DEG C, 106 DEG C, 110 DEG C or 115 DEG C etc..
In the spray drying cladding process, the solid content of the slurry for being spray-dried is 10wt%~30wt%, for example
Can be 10wt%, 12wt%, 15wt%, 17wt%, 20wt%, 22wt%, 24wt%, 26wt%, 28wt% or 30wt% etc..
In the spray drying cladding process, the feed rate of mixed slurry is 10mL/min~40mL/ during spray drying
Min, for example can for 10mL/min, 15mL/min, 18mL/min, 20mL/min, 25mL/min, 30mL/min, 33mL/min,
36mL/min or 40mL/min etc..
Preferably, step (3) it is described second carbonization carry out in an inert atmosphere, the inert atmosphere include nitrogen atmosphere,
In argon gas atmosphere, neon atmosphere, helium atmosphere, xenon atmosphere or Krypton atmosphere any one or at least two combination.
Preferably, step (3) it is described second carbonization temperature be 900 DEG C~1100 DEG C, for example can for 900 DEG C, 920 DEG C,
940 DEG C, 960 DEG C, 985 DEG C, 1000 DEG C, 1025 DEG C, 1050 DEG C, 1080 DEG C or 1100 DEG C etc..
Preferably, step (3) it is described second carbonization time be 2h~4h, for example can for 2h, 2.5h, 3h, 3.2h,
3.5h, 3.6h, 3.8h or 4h etc..
Preferably, during the temperature of step (2) second carbonization is warmed up to from the temperature of the first carbonization, heat up speed
Rate be 1 DEG C/min~10 DEG C/min, for example can for 1 DEG C/min, 3 DEG C/min, 5 DEG C/min, 6 DEG C/min, 7 DEG C/min, 8 DEG C/
Min, 9 DEG C/min or 10 DEG C/min etc..
The third aspect, the present invention provides a kind of negative material, and the negative material is that the carbon silicon described in first aspect is combined
Material.
Fourth aspect, the present invention provides a kind of lithium ion battery, and the lithium ion battery is included as described in relation to the first aspect
Carbon-silicon composite material is used as negative material.
Compared with prior art, the invention has the advantages that:
(1) present invention can be converted into the adhesive of pyrolytic carbon from through being carbonized, by first with adhesive to amorphous carbon
Surface modification is carried out, then the further composite Nano silicon under the adhesive effect of adhesive, is carbonized then at relatively low temperature control one
After carry out carbon source cladding, be finally carbonized in temperature control two higher, obtain carbon-silicon composite material.Method of the present invention operation letter
It is single, it is adapted to large-scale production.
(2) in carbon-silicon composite material of the invention, on the one hand adding for binding agent improve amorphous carbon and nano-silicon
Active force, it is suppressed that silicon nanoparticle from agglomeration so that nano-silicon can equably be compound to amorphous carbon material table
Face, the bulk effect of silicon and the influence to its structure during the de- lithium of reduction;On the other hand, binding agent is converted in carbonisation
It is pyrolytic carbon, the pyrolytic carbon converted with carbon source cooperatively coats nano-silicon so as to improve the degree that is wrapped by of nano-silicon, wraps
Cover that effect is good, can effectively suppress the expansion of silicon, improve the chemical properties such as cycle performance.And, it is dispersed with the heat of nano-silicon
Solution carbon forms conductive network, compensate for the inferior position of silicon poorly conductive, is conducive to playing and improving the capacity and first effect of silicon.
(3) Stability Analysis of Structures of carbon-silicon composite material that the present invention is prepared, nano-silicon is uniformly dispersed and is wrapped by degree
It is very high, the negative material of lithium ion battery is highly suitable as, battery is made using carbon-silicon composite material of the invention, show
De- lithium specific capacity very high, good cycle and fills excellent soon, takes off lithium specific capacity in more than 391.7mAh/g, and 1.0C is permanent
More than 95.3%, 10min charge rates are up to 90.2% for stream 50 capability retentions of discharge and recharge.