CN1558463A - Preparation method of in-situ thermal crosslinking of fluorine-containing gel electrolyte material and preparation method of polymer lithium-ion battery - Google Patents
Preparation method of in-situ thermal crosslinking of fluorine-containing gel electrolyte material and preparation method of polymer lithium-ion battery Download PDFInfo
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- CN1558463A CN1558463A CNA2004100160365A CN200410016036A CN1558463A CN 1558463 A CN1558463 A CN 1558463A CN A2004100160365 A CNA2004100160365 A CN A2004100160365A CN 200410016036 A CN200410016036 A CN 200410016036A CN 1558463 A CN1558463 A CN 1558463A
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Abstract
The invention provides a method of making fluorine-containing gel state electrolyte material and polymeric lithium ion cells by employing in-situ thermal cross bonding process, wherein fluorine-containing acrylic ester material is used as monomer, and double functional group acrylic acid ester containing polyethylene glycol or triple functional group acrylic acid ester containing polyethylene glycol are used as cross linking agent, the making process comprises injecting the miscible liquid comprising monomer, cross linking agent, thermal initiation agent and lithium ion electrolyte salt solution into the core of lithium ion cells, heating the cell to result in-situ thermal chemical cross-linking for the two acrylic esters, whereby the acrylic ester copolymer network bundles the solution in the electrolyte, forming the gel state electrolyte material with stabilized physical and chemical properties.
Description
Technical field
The invention belongs to the fluoride gel attitude electrolyte of polymer Li-ion battery and the manufacture method of battery thereof.
Background technology
Can produce the liquid electrolyte lithium ion battery in a large number both at home and abroad at present, the liquid electrolyte lithium ion battery adopts the organic bath liquid that contains lithium salts, and its composition is mainly by ethylmethyl carbonate (ethylmethyl carbonate (EMC), C
4H
8O
3), ethylene carbonate (ethylenecarbonate (EC), C
3H
4O
3), diethyl carbonate (diethyl carbonate (DEC), C
5H
10O
3), dimethyl carbonate (dimethyl carbonate (DMC), C
3H
6O
3), propene carbonate (propylenecarbonate (PC), C
4H
6O
3) and vinylene carbonate (vinylene carbonate (VC), C
3H
2O
3) wait organic solvent and various inorganic lithium salt such as LiCF
3SO
3, LiN (CF
3SO
2)
2, LiC (CF
3SO
2)
3, LiPF
6, LiBF
4, LiAsF
6And LiClO
4Deng the solution that is mixed with is electrolyte solution.These lithium salt solutions provide conductivity near 10 for lithium ion battery
-2The electrolyte solution of S/cm has satisfied the requirement that lithium ion battery hangs down internal resistance, high charge-discharge magnification.The weak point of liquid lithium ionic cell be adopted volatile, inflammable, easily flow thereby the organic solution of easy to leak, if improper use, might cause danger such as leakage, corrosion and burning, so the liquid electrolyte lithium ion battery adopts all generally metal material to make shell to improve fail safe.Adopt at present aluminum-plastic composite material softer packing technique to prepare that liquid lithium ionic cell also exists leakage and the problem of flatulence took place between the storage life.
The polymer Li-ion battery of a new generation is tried hard in the advantage that keeps the liquid electrolyte lithium ion battery, overcome above-mentioned shortcoming, the representative of this respect is with the invention (U.S.patent5 of Bellcore company, 540,741) usefulness vinylidene difluoride-hexafluoropropylene copolymer (PVDF-HFP) is the perforated membrane technology (physical crosslinking method) and the gel state electrolyte material technology (US patents 5603982) (Chemical Crosslinking Methods) of material, and these technology are wrapped in liquid electrolyte in polymer micro or the network.Polymer Li-ion battery has been simplified the battery case packing, make large tracts of land, ultrathin type, lithium ion battery different and high-energy-density become possibility, and be used for portable electric appts of new generation in a large number as energy source device, but the expensive polymer dielectric film manufacturing process that needs complex process in this kind battery production process becomes the technical bottleneck of making polymer Li-ion battery.
The fluoro containing polymers network configuration is the characteristics that the electrolyte of gel state has stable electrochemical property, but fluoro containing polymers network parcel electrolyte ability is relatively poor, and solution leakage can take place longer-term storage.
The macromolecule network that contains the polyethylene glycol multi-functional acrylate has the ability of good parcel electrolyte, the network bonds chalaza that forms with chemical bond has good temperature stability, can keep the electrolyte long term storage behind the gel and the problem of solution leakage does not take place.
Fluorinated acrylate monomer, contain and form the electrolytical mixed liquor precursor of fluoride gel attitude after polyethylene glycol multi-functional acrylate crosslinking agent and thermal initiator are dissolved in lithium ion battery electrolyte solution commonly used, heating make monomer in this mixed liquor and crosslinking agent realize crosslinked after, copolymer networks parcel electrolyte forms the gel polymer electrolyte material, it has the characteristics of stable physical property and stable electrochemical property concurrently, is applicable to the needs of gel state electrolyte polymer Li-ion battery.
Summary of the invention
The objective of the invention is to obtain a kind of prepare simple, technology is convenient, overcome the preparation method of not enough fluoride gel attitude electrolyte such as current electrolysis matter liquid seepage, volatilization, the degassing.
The objective of the invention is to develop a kind of manufacture method of using the polymer Li-ion battery of above-mentioned fluoride gel attitude electrolyte.
The present invention is monomer with the fluorinated acrylate, is crosslinking agent with the multi-functional acrylate who contains polyethylene glycol, forms mixed liquor after monomer, crosslinking agent and thermal initiator are dissolved in electrolyte solution.Above-mentioned mixed liquor is injected lithium ion battery cell, this mixed liquor has good flowability before polymerization, the battery battery core that contains this mixed liquor by heating makes monomer and crosslinking agent generation thermochemical crosslinking on the throne in cell body, electrolyte solution then is wrapped in the copolymer networks, forms the gel state electrolyte material of physics and stable electrochemical property and makes fluorine-containing gel state electrolyte polymer Li-ion battery simultaneously.
It is monomer that the present invention adopts fluorinated acrylate, and the multi-functional acrylate who contains polyethylene glycol is crosslinking agent, and the thermal polymerization temperature is 60-80 ℃, and the time is 60-180 minute.The polymer that thermal polymerization forms possesses three-dimensional net structure, and the gained gel rubber system has big electrolyte solution to contain ability and stable temperature characterisitic.Gained gel polymer electrolyte material keeps the characteristics of liquid lithium ion electrolyte solution high conductivity, and by regulating the amount of monomer and crosslinking agent, the gel state electrolyte conductivity of electrolyte materials when making 25 ℃ is greater than 4 * 10
-3S/cm, and the conductivity subzero 20 ℃ the time is greater than 1 * 10
-3S/cm, gel polymer electrolyte fusing point (T simultaneously
m) be higher than 85 ℃, the safety problem that has overcome liquid electrolyte lithium ion battery electrolyte solution easy to leak, volatile, easy flatulence and brought thus.
The fluorinated acrylate monomer that the present invention adopts comprises:
Structural formula is H
2C=C (R
1) CO
2R
2Compound, R wherein
1The structure of group is H or CH
3R
2Unit structure is CH
2CH
2(CF
2)
mCF
3, CH
2(CF
2)
mCF
3, CH
2(CF
2)
mCHF
2, CH
2CH
2(CF
2)
mCF (CF
3)
2, CH
2CF
2CH (F) CF
3Deng, m=0-9.Fluorinated acrylate monomer weight accounts for the 2-25Wt% of electrolyte mixed liquor total weight.
Multi-functional acrylate's crosslinking agent that the present invention adopts comprise contain polyethylene glycol two, the acrylate of trifunctional.
Acrylate cross linked dose the structural formula that contains the difunctional of polyethylene glycol is: H
2C=C (R
1) CO
2(CH
2CH
2O)
n-R-(CH
2CH
2O)
n, OCC (R
1)=CH
2, R wherein
1The structure of group is H or CH
3The structure of R group is (CH
2CH
2O)
m, SiH
2, Si (CH
3)
2Or Si (OCH
3)
2n=0-10,n’=0-10,m=0-10。
Acrylate cross linked dose of difunctional that contains polyethylene glycol also can have phenyl ring, and its structural formula is:
[H
2C=C (R
1) CO
2(CH
2CH
2O)
nC
6H
4]
2C (CH
3)
2, R wherein
1The structure of group is H or CH
3, n=0-10, C
6H
4Be phenyl ring.
The structural formula that contains trifunctional group acrylate's crosslinking agent of polyethylene glycol is:
[CH
2=C (R
1) CO
2(CH
2CH
2O)
nCH
2]
3CR, wherein R
1The structure of group is H or CH
3, the value of n is between 0-15, and the structure of R group is CH
3Or C
2H
5
Above multi-functional acrylate's crosslinking agent weight accounts for the 2-15Wt% of electrolyte mixed liquor total weight.
Fluorinated acrylate monomer of the present invention as:
H
2C=C (CH
3) CO
2CH
2CF
3(HFC-143a ylmethyl acrylate, Trifluoroethylmethacrylate), H
2C=CHCO
2CH
2CF
3(HFC-143a base acrylate, Trifluoroethylacrylate), H
2C=C (CH
3) CO
2CH
2CF
2CHF
2(tetrafluoropropane ylmethyl acrylate, Tetrfluoropropyl methacrylate), H
2C=CHCO
2CH
2CF
2CHF
2(tetrafluoropropane base acrylate, Tetrfluoropropyl acrylate), H
2C=C (CH
3) CO
2CH
2CF
2CF
3(pentafluoropropane ylmethyl acrylate, Pentafluoropropyl methacrylate), H
2C=CHCO
2CH
2CF
2CF
3(pentafluoropropane base acrylate, Pentafluoropropyl acrylate), H
2C=C (CH
3) CO
2CH (CF
3)
2(the different propyl methacrylate of hexafluoro, Hexafluoroisopropyl methacrylate), H
2C=C (CH
3) CO
2CH
2CF
2CH (F) CF
3(hexafluoro butane ylmethyl acrylate, Hexafluorobutylmethacrylate), H
2C=CHCO
2CH
2CF
2CH (F) CF
3(hexafluoro butane base acrylate, Hexafluorobutyl acrylate), H
2C=C (CH
3) CO
2CH
2CF
2CF
2CF
3(seven fluorine butane group methacrylates, Heptafluorobutyl metharcylate), H
2C=CHCO
2CH
2CF
2CF
2CF
3(seven fluorine butane group acrylate, Heptafluorobutyl arcylate), H
2C=C (CH
3) CO
2CH
2CH
2(CF
2)
6CF (CF
3)
2(ten hexafluoros-(trifluoromethyl) decyl methacrylate, Hexadecafluoro-(trifluoromethyl) decyl methacrylate), H
2C=CHCO
2CH
2CH
2(CF
2)
6CF (CF
3)
2(ten hexafluoros-(trifluoromethyl) decyl acrylate, Hexadecafluoro-(trifluoromethyl) decyl acrylate), H
2C=C (CH
3) CO
2CH
2(CF
2)
7CHF
2(ten hexafluoro nonyl methacrylates, Hexadecafluorononyl methacrylate), H
2C=CHCO
2CH
2CH
2(CF
2)
7CHF
2(ten hexafluoro nonyl acrylate, Hexadecafluorononyl acrylate), H
2C=C (CH
3) CO
2CH
2CH
2(CF
2)
7CF
3(17 fluorine decyl methacrylates, Heptadecafluorodecyl methacrylate), H
2C=CHCO
2CH
2CH
2(CF
2)
7CF
3(17 fluorine decyl acrylate, Heptadecafluorodecyl acrylate), H
2C=C (CH
3) CO
2CH
2CH
2(CF
2)
9CF
3(21 fluorine dodecyl methyl acrylate, Heneicosafluorododecyl methacrylate) and H
2C=CHCO
2CH
2CH
2(CF
2)
9CF
3(21 fluorine dodecyl acrylate, Heneicosafluorododecyl acrylate) etc.
Bifunctional acrylate's crosslinking agent of polyethylene glycol of the present invention is as H
2C=CHCO
2(CH
2CH
2O)
1OCCH=CH
2(glycol diacrylate, ethylene glycoldiacrylate), H
2C=C (CH
3) CO
2(CH
2CH
2O)
1OCC (CH
3)=CH
2(ethylene glycol dimethacrylate, ethylene glycol dimethacrylate), H
2C=CHCO
2(CH
2CH
2O)
2OCCH=CH
2(diethylene glycol diacrylate, Di (ethylene glycol) diacrylate), H
2C=C (CH
3) CO
2(CH
2CH
2O)
2OCC (CH
3)=CH
2(diethylene glycol dimethylacrylate, Di (ethylene glycol) dimethacrylate), H
2C=CHCO
2(CH
2CH
2O)
3OCCH=CH
2(triethylene glycol diacrylate, Tri (ethylene glycol) diacrylate), H
2C=C (CH
3) CO
2(CH
2CH
2O)
3OCC (CH
3)=CH
2(triethylene glycol dimethylacrylate, Tri (ethylene glycol) dimethacrylate), H
2C=CHCO
2(CH
2CH
2O)
4OCCH=CH
2(tetraethylene glycol diacrylate, Tetra (ethylene glycol) diacrylate), H
2C=C (CH
3) CO
2(CH
2CH
2O)
4OCC (CH
3)=CH
2(TEG dimethylacrylate, Tetra (ethylene glycol) dimethacrylate), H
2C=CHCO
2(CH
2CH
2O)
nOCCH=CH
2(polyethyleneglycol diacrylate, Poly (ethyleneglycol) diacrylate, n=5-20), H
2C=C (CH
3) CO
2(CH
2CH
2O)
nOCC (CH
3)=CH
2(polyethylene glycol dimethacrylate, Poly (ethylene glycol) dimethacrylate, n=5-20).
Acrylate cross linked dose of difunctional that contains polyethylene glycol and phenyl ring is:
(H
2C=CHCO
2(CH
2CH
2O)
nC
6H
4)
2C (CH
3)
2(bisphenol-A ethoxyquin (1 EO/phenol) diacrylate, Bisphenol A ethoxylate (1 EO/phenol) diacrylate), (H
2C=CHCO
2(CH
2CH
2O)
nC
6H
4)
2CH
2(bisphenol-A ethoxyquin (2 EO/phenol) diacrylate, Bisphenol Aethoxylate (2 EO/phenol) diacrylate), (H
2C=C (CH
3) CO
2(CH
2CH
2O)
nC
6H
4)
2C (CH
3)
2(bisphenol-A ethoxyquin (2 EO/phenol) dimethylacrylate, Bisphenol A ethoxylate (2 EO/phenol) dimethacrylate), (H
2C=CHCO
2(CH
2CH
2O)
nC
6H
4)
2C (CH
3)
2(bisphenol-A ethoxyquin (4 EO/phenol) diacrylate, BisphenolA ethoxylate (4 EO/phenol) diacrylate), (H
2C=C (CH
3) CO
2(CH
2CH
2O)
nC
6H
4)
2C (CH
3)
2(bisphenol-A ethoxyquin (4 EO/phenol) dimethylacrylate, Bisphenol A ethoxylate (4 EO/phenol) dimethacrylate), (H
2C=C (CH
3) CO
2(CH
2CH
2O)
nC
6H
4)
2C (CH
3)
2(bisphenol-A ethoxyquin (15 EO/phenol) dimethylacrylate, Bisphenol A ethoxylate (15 EO/phenol) dimethacrylate) etc.
The trifunctional group acrylate's crosslinking agent that contains polyethylene glycol of the present invention as:
Ethoxyquin trimethylolpropane triacrylate (Trimethylolpropane ethoxylate (EO/OH) Triacrylate (1 EO/OH-TMPTA), ethoxyquin trimethylolpropane triacrylate (Trimethylolpropane ethoxylate (EO/OH) Triacrylate (7/3 EO/OH-TMPTA) and ethoxyquin trimethylolpropane triacrylate (Trimethylolpropane ethoxylate (EO/OH) Triacrylate (14/3 EO/OH-TMPTA) etc.
The thermal initiator that is used for preparing the gel electrolyte polymerization reaction is a free radical polyaddition reaction thermal initiator commonly used, can be: dibenzoyl peroxide ((C
6H
5CO
2)
2, BPO), peroxidating two (o-methyl-benzene formyl) ((CH
3C
6H
4CO
2)
2), acetyl peroxide isobutyryl (CH
3CO-O-O-COCH (CH
3)
2), di-isopropyl peroxydicarbonate (((CH
3)
2CHOCO
2)
2), di-cyclohexylperoxy di-carbonate ((C
6H
11OCO
2)
2), peroxy dicarbonate two (4-tert-butyl group cyclohexyl) (((CH
3)
3CC
6H
10OCO
2)
2) and the peroxidating pivalic acid tert-butyl ester ((CH
3)
3C-CO-O-O-C (CH
3)
3), azodiisobutyronitrile ((CH
3(CH
3) C (CN) N)
2, AIBN), 2,2'-Azobis(2,4-dimethylvaleronitrile) ((CH
3)
2CHCH
2(CH
3) C (CN) N)
2) etc.Thermal initiator weight accounts for the 0.1-3Wt% of electrolyte mixed liquor total weight.
The liquid lithium ion electrolyte salt solution is: 1M LiPF
6, EC/DEC=1/1 (W/W), 1MLiPF
6, EC/DEC/VC=1/1/0.1 (W/W/W), 1M LiPF
6, EC/DMC=1/1 (W/W), 1MLiPF
6, EC/DMC/VC=1/1/0.1 (W/W/W), 1M LiPF
6, EC/PC=1/1 (W/W), 1MLiPF
6, EC/PC/VC=1/1/0.1 (W/W/W), 1M LiPF
6, EC/DEC/PC=1/1/1 (W/W/W), 1M LiPF
6, EC/DEC/PC/VC=1/1/1/0.1 (W/W/W/W), 1M LiPF
6, EC/DEC/DMC=1/1/1 (W/W/W), 1M LiPF
6, EC/DEC/DMC/VC=1/1/1/0.1 (W/W/W/W); 1M LiPF
6, EC/DMC/EMC=1/1/1 (W/W/W), 1MLiPF
6, EC/DMC/EMC/VC=1/1/1/0.1 (W/W/W/W).
Above-mentioned reactant feed, promptly each components contents of mixed liquor of compositions such as monomer, crosslinking agent, initator, lithium-ion electrolyte salting liquid is as follows:
Fluorinated acrylate monomer: 2-25Wt%;
The multi-functional acrylate's crosslinking agent that contains polyethylene glycol: 2-15Wt%;
Thermal initiator: 0.1-3Wt%;
Liquid lithium ion electrolyte salt solution: 70-95Wt%.
Above-mentioned fluorinated acrylate monomer and contain polyethylene glycol multi-functional acrylate crosslinking agent and be dissolved in and form gel state electrolyte mixed liquor precursor behind the electrolyte solution, copolymerization does not take place in room temperature in mixed liquor below 25 ℃, and maintenance low-viscosity in the quite a long time is arranged, help mixed liquor and evenly injected battery.The mixed liquor that monomer, crosslinking agent, initator, lithium-ion electrolyte salting liquid are formed injects by the vacuum liquid-injection equipment in the battery container of the lithium ion battery cell that is made of positive pole band, negative pole band and diaphragm material, and the heating battery housing makes this mixed liquor generation cross-linking reaction form fluoride gel attitude electrolyte and makes polymer Li-ion battery simultaneously.
The thermal polymerization temperature is better in 65-75 ℃ of scope, has promptly both guaranteed the formation of gel, and the side reaction of having avoided high temperature to cause has again simultaneously guaranteed the performance of product.
Polymer Li-ion battery packing forms of the present invention can be column type, flat box-shaped, thin slice shape or other polymorphic structure, is convenient to the use of various complete machines.
Battery container material of the present invention is aluminium foil-plastics multilayer complex films.
The combining structure form of inside battery anode electrode band, barrier film and negative electrode band can adopt coiling form or lamination form.It is two-sided that cathode film is applied to aluminium foil, and positive electrode active materials is lithium and cobalt oxides (LiCoO
2), lithium manganese oxide (LiMn
2O
4) or lithium-cobalt-nickel oxide (LiNi
xCo
1-xO
2, x=0-1), conductive agent is acetylene black or electrically conductive graphite powder, binding agent is the mixture of polyvinylidene fluoride (PVDF) or polyvinylidene fluoride (PVDF) and polyacrylate.It is two-sided that negative electrode film is applied to Copper Foil, and negative active core-shell material is carbosphere (MCMB), Delanium or the mixture of the two, and conductive agent is an acetylene black, and binding agent is the mixture of polyvinylidene fluoride (PVDF) or polyvinylidene fluoride (PVDF) and polyacrylate.
Battery diaphragm adopts the nonwoven fabrics or the perforated membrane of polypropylene (PP), polyethylene (PE) or vinylidene difluoride-hexafluoropropylene copolymer material such as (PVDF-HPF), thickness 10-25 micron, and preferably thickness is at the 10-15 micron, and porosity is greater than 35%.
The inventive method preparation method is simple, and technological requirement is convenient.Because monomer in the inventive method, crosslinking agent, electrolyte solution, initator are as the precursor of gel state electrolyte mixed liquor, therefore very at room temperature mixed liquor has good flowability in the long duration, is suitable for making in the automation electrolyte solution perfusion equipment of battery using.Conductivity during 25 ℃ of gel state electrolyte materials that the inventive method is made is greater than 4 * 10
-3S/cm, and the conductivity subzero 20 ℃ the time is greater than 1 * 10
-3S/cm, gel polymer electrolyte fusing point (T simultaneously
m) be higher than 85 ℃, make battery have low internal resistance and high specific energy density, the adverse consequences that it has been avoided electrolyte solution seepage, volatilization, flatulence effectively and has brought thus has a good application prospect.
Embodiment
Example 1 in-situ heat cross bonding legal system is equipped with the manufacture method 1 of fluoride gel attitude electrolyte and polymer Li-ion battery
HFC-143a ylmethyl acrylate (H
2C=C (CH
3) CO
2CH
2CF
3): 10Wt%;
Ethylene glycol dimethacrylate (H
2C=C (CH
3) CO
2(CH
2CH
2O)
1OCC (CH
3)=CH
2): 3Wt%;
Dibenzoyl peroxide ((C
6H
5CO
2)
2, BPO): 0.25Wt%;
Electrolyte solution, 1M liPF
6, EC/DEC/VC=1/1/0.1 (W/W/W): 86.75Wt%.
Under dry environment (relative humidity is lower than 2%) and room temperature situation, by above-mentioned percentage by weight preparation mixed liquor.Mixed liquor should become transparence and good flowability is arranged, adopt vacuum impregnation, the mixed liquor injection is contained the battery cell body of (battery contains anodal band, negative pole band, barrier film and positive and negative lug), make positive electrode, negative material and barrier film absorb mixed liquor, follow the thermal polymerization of carrying out on the throne, polymerization temperature 65-75 ℃, time 60-180 minute, mobile liquid electrolyte was transformed into gel state electrolyte and makes the gel state electrolyte polymer Li-ion battery thus.
Example 2 in-situ heat cross bonding legal systems are equipped with the manufacture method 2 of fluoride gel attitude electrolyte and polymer Li-ion battery
Tetrafluoropropane ylmethyl acrylate (H
2C=C (CH
3) CO
2CH
2CF
2CHF
2): 8Wt%;
Triethylene glycol dimethylacrylate (CH
2=C (CH
3) CO
2(CH
2CH
2O)
3OCC (CH
3)=CH
2): 3Wt%;
Azodiisobutyronitrile ((CH
3(CH
3) C (CN) N)
2, AIBN): 0.3Wt%;
Electrolyte solution, 1M liPF
6, EC/DEC=1/1 (W/W): 88.7Wt%.
Under dry environment (relative humidity is lower than 2%) and room temperature situation, by above-mentioned percentage by weight preparation mixed liquor.Mixed liquor should become transparence and good flowability is arranged, adopt vacuum impregnation, the mixed liquor injection is contained the battery cell body of (battery contains anodal band, negative pole band, barrier film and positive and negative lug), make positive electrode, negative material and barrier film absorb mixed liquor, then carry out thermal polymerization on the throne, polymerization temperature 65-75 ℃, time 60-180 minute, mobile liquid electrolyte was transformed into gel state electrolyte and makes the gel state electrolyte polymer Li-ion battery thus.
Example 3 in-situ heat cross bonding legal systems are equipped with the manufacture method 3 of fluoride gel attitude electrolyte and polymer Li-ion battery
Pentafluoropropane ylmethyl acrylate (H
2C=C (CH
3) CO
2CH
2CF
2CF
3): 10wt%;
Ethoxyquin trimethylolpropane triacrylate (7/3 EO/OH TMPTA): 2.25Wt%;
Peroxy dicarbonate two (4-tert-butyl group cyclohexyl) (((CH
3)
3CC
6H
10OCO
2)
2): 0.25Wt%;
Electrolyte solution, 1M liPF
6, EC/DEC/DMC=1/1/1 (W/W/W): 87.5Wt%.
Under dry environment (relative humidity is lower than 2%) and room temperature situation, by above-mentioned percentage by weight preparation mixed liquor.Mixed liquor should become transparence and good flowability is arranged, adopt vacuum impregnation, the mixed liquor injection is contained the battery cell body of (battery contains anodal band, negative pole band, barrier film and positive and negative lug), make positive electrode, negative material and barrier film absorb mixed liquor, then carry out thermal polymerization on the throne, polymerization temperature 65-75 ℃, time 60-180 minute, mobile liquid electrolyte was transformed into gel state electrolyte and makes the gel state electrolyte polymer Li-ion battery thus.
Example 4 in-situ heat cross bonding legal systems are equipped with the manufacture method 4 of fluoride gel attitude electrolyte and polymer Li-ion battery
The different propyl methacrylate of hexafluoro (H
2C=C (CH
3) CO
2CH (CF
3)
2): 8Wt%:
Bisphenol-A ethoxyquin (4 EO/phenol) dimethylacrylate: 4Wt%:
Azodiisobutyronitrile ((CH
3(CH
3) C (CN) N)
2, AIBN): 0.3Wt%:
Electrolyte solution, 1M liPF
6, EC/DEC/DMC/VC=1/1/1/0.1 (W/W/W/W): 87.7Wt%.
Under dry environment (relative humidity is lower than 2%) and room temperature situation, by above-mentioned percentage by weight preparation mixed liquor.Mixed liquor should become transparence and good flowability is arranged, adopt vacuum impregnation, the mixed liquor injection is contained the battery cell body of (battery contains anodal band, negative pole band, barrier film and positive and negative lug), make positive electrode, negative material and barrier film absorb mixed liquor, then carry out thermal polymerization on the throne, polymerization temperature 65-75 ℃, time 60-180 minute, mobile liquid electrolyte was transformed into gel state electrolyte and makes the gel state electrolyte polymer Li-ion battery thus.
Example 5 in-situ heat cross bonding legal systems are equipped with the manufacture method 5 of fluoride gel attitude electrolyte and polymer Li-ion battery
Hexafluoro butane base acrylate (H
2C=CHCO
2CH
2CF
2CH (F) CF
3): 8Wt%:
Bisphenol-A ethoxyquin (15 EO/phenol) dimethylacrylate: 3.5Wt%:
Peroxy dicarbonate two (4-tert-butyl group cyclohexyl) (((CH
3)
3CC
6H
10OCO
2)
2): 0.5Wt%;
Electrolyte solution, 1M liPF
6, EC/DMC/EMC/VC=1/1/1/0.1 (W/W/W/W): 88Wt%;
Under dry environment (relative humidity is lower than 2%) and room temperature situation, by above-mentioned percentage by weight preparation mixed liquor.Mixed liquor should become transparence and good flowability is arranged, adopt vacuum impregnation, the mixed liquor injection is contained the battery cell body of (battery contains anodal band, negative pole band, barrier film and positive and negative lug), make positive electrode, negative material and barrier film absorb mixed liquor, then carry out thermal polymerization on the throne, polymerization temperature 65-75 ℃, time 60-180 minute, mobile liquid electrolyte was transformed into gel state electrolyte and makes the gel state electrolyte polymer Li-ion battery thus.
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