WO2023115625A1 - Separator having large elastic deformation quantity and preparation method therefor - Google Patents
Separator having large elastic deformation quantity and preparation method therefor Download PDFInfo
- Publication number
- WO2023115625A1 WO2023115625A1 PCT/CN2021/142772 CN2021142772W WO2023115625A1 WO 2023115625 A1 WO2023115625 A1 WO 2023115625A1 CN 2021142772 W CN2021142772 W CN 2021142772W WO 2023115625 A1 WO2023115625 A1 WO 2023115625A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- elastic deformation
- condition
- preparation
- base film
- coating
- Prior art date
Links
- 230000005489 elastic deformation Effects 0.000 title claims abstract description 62
- 238000002360 preparation method Methods 0.000 title claims abstract description 31
- 238000000034 method Methods 0.000 claims abstract description 33
- 239000011248 coating agent Substances 0.000 claims abstract description 29
- 238000000576 coating method Methods 0.000 claims abstract description 29
- 230000008569 process Effects 0.000 claims abstract description 23
- 239000000919 ceramic Substances 0.000 claims description 17
- 239000002245 particle Substances 0.000 claims description 16
- 229920000098 polyolefin Polymers 0.000 claims description 16
- 239000012528 membrane Substances 0.000 claims description 14
- 238000001035 drying Methods 0.000 claims description 13
- 238000001125 extrusion Methods 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 10
- 239000006255 coating slurry Substances 0.000 claims description 9
- 229930195733 hydrocarbon Natural products 0.000 claims description 9
- 150000002430 hydrocarbons Chemical class 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 9
- 239000002994 raw material Substances 0.000 claims description 9
- 229920005672 polyolefin resin Polymers 0.000 claims description 8
- 239000002904 solvent Substances 0.000 claims description 8
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 claims description 7
- 229910001416 lithium ion Inorganic materials 0.000 claims description 7
- 238000002844 melting Methods 0.000 claims description 7
- 230000008018 melting Effects 0.000 claims description 7
- 238000005266 casting Methods 0.000 claims description 6
- 239000002033 PVDF binder Substances 0.000 claims description 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 5
- 229920006231 aramid fiber Polymers 0.000 claims description 5
- 229920000620 organic polymer Polymers 0.000 claims description 5
- 229920002981 polyvinylidene fluoride Polymers 0.000 claims description 5
- 239000007787 solid Substances 0.000 claims description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 4
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 4
- 239000002861 polymer material Substances 0.000 claims description 4
- 238000004321 preservation Methods 0.000 claims description 4
- 238000007493 shaping process Methods 0.000 claims description 4
- 239000004215 Carbon black (E152) Substances 0.000 claims description 3
- 239000004642 Polyimide Substances 0.000 claims description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 3
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims description 3
- 239000000654 additive Substances 0.000 claims description 3
- 238000010828 elution Methods 0.000 claims description 3
- 239000011268 mixed slurry Substances 0.000 claims description 3
- 229920001721 polyimide Polymers 0.000 claims description 3
- 239000000843 powder Substances 0.000 claims description 3
- 230000001360 synchronised effect Effects 0.000 claims description 3
- 238000011282 treatment Methods 0.000 claims description 3
- FRWYFWZENXDZMU-UHFFFAOYSA-N 2-iodoquinoline Chemical compound C1=CC=CC2=NC(I)=CC=C21 FRWYFWZENXDZMU-UHFFFAOYSA-N 0.000 claims description 2
- 229910052580 B4C Inorganic materials 0.000 claims description 2
- 229910052582 BN Inorganic materials 0.000 claims description 2
- PZNSFCLAULLKQX-UHFFFAOYSA-N Boron nitride Chemical compound N#B PZNSFCLAULLKQX-UHFFFAOYSA-N 0.000 claims description 2
- 239000004697 Polyetherimide Substances 0.000 claims description 2
- 229910052581 Si3N4 Inorganic materials 0.000 claims description 2
- NRTOMJZYCJJWKI-UHFFFAOYSA-N Titanium nitride Chemical compound [Ti]#N NRTOMJZYCJJWKI-UHFFFAOYSA-N 0.000 claims description 2
- 229910026551 ZrC Inorganic materials 0.000 claims description 2
- OTCHGXYCWNXDOA-UHFFFAOYSA-N [C].[Zr] Chemical compound [C].[Zr] OTCHGXYCWNXDOA-UHFFFAOYSA-N 0.000 claims description 2
- LTPBRCUWZOMYOC-UHFFFAOYSA-N beryllium oxide Inorganic materials O=[Be] LTPBRCUWZOMYOC-UHFFFAOYSA-N 0.000 claims description 2
- 229910001593 boehmite Inorganic materials 0.000 claims description 2
- INAHAJYZKVIDIZ-UHFFFAOYSA-N boron carbide Chemical compound B12B3B4C32B41 INAHAJYZKVIDIZ-UHFFFAOYSA-N 0.000 claims description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 2
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims description 2
- 239000000292 calcium oxide Substances 0.000 claims description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 2
- PMHQVHHXPFUNSP-UHFFFAOYSA-M copper(1+);methylsulfanylmethane;bromide Chemical compound Br[Cu].CSC PMHQVHHXPFUNSP-UHFFFAOYSA-M 0.000 claims description 2
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 claims description 2
- GDVKFRBCXAPAQJ-UHFFFAOYSA-A dialuminum;hexamagnesium;carbonate;hexadecahydroxide Chemical compound [OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Al+3].[Al+3].[O-]C([O-])=O GDVKFRBCXAPAQJ-UHFFFAOYSA-A 0.000 claims description 2
- KZHJGOXRZJKJNY-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Si]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O KZHJGOXRZJKJNY-UHFFFAOYSA-N 0.000 claims description 2
- 239000000835 fiber Substances 0.000 claims description 2
- 229920006270 hydrocarbon resin Polymers 0.000 claims description 2
- 229910001701 hydrotalcite Inorganic materials 0.000 claims description 2
- 229960001545 hydrotalcite Drugs 0.000 claims description 2
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 claims description 2
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 claims description 2
- 239000000347 magnesium hydroxide Substances 0.000 claims description 2
- 229910001862 magnesium hydroxide Inorganic materials 0.000 claims description 2
- 239000000395 magnesium oxide Substances 0.000 claims description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 2
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 claims description 2
- 239000000155 melt Substances 0.000 claims description 2
- 229910052901 montmorillonite Inorganic materials 0.000 claims description 2
- 229910052863 mullite Inorganic materials 0.000 claims description 2
- 229920003229 poly(methyl methacrylate) Polymers 0.000 claims description 2
- 229920002492 poly(sulfone) Polymers 0.000 claims description 2
- 229920005569 poly(vinylidene fluoride-co-hexafluoropropylene) Polymers 0.000 claims description 2
- 229920002239 polyacrylonitrile Polymers 0.000 claims description 2
- 229920001601 polyetherimide Polymers 0.000 claims description 2
- 239000004926 polymethyl methacrylate Substances 0.000 claims description 2
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 claims description 2
- 229910010271 silicon carbide Inorganic materials 0.000 claims description 2
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 claims description 2
- 229910052596 spinel Inorganic materials 0.000 claims description 2
- 239000011029 spinel Substances 0.000 claims description 2
- 239000000725 suspension Substances 0.000 claims description 2
- 239000004408 titanium dioxide Substances 0.000 claims description 2
- 229920003171 Poly (ethylene oxide) Polymers 0.000 claims 1
- 230000000996 additive effect Effects 0.000 claims 1
- 239000000377 silicon dioxide Substances 0.000 claims 1
- 235000012239 silicon dioxide Nutrition 0.000 claims 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 abstract description 6
- 229910052744 lithium Inorganic materials 0.000 abstract description 6
- 230000000704 physical effect Effects 0.000 abstract description 6
- 230000004048 modification Effects 0.000 abstract description 4
- 238000012986 modification Methods 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract 1
- 230000002427 irreversible effect Effects 0.000 abstract 1
- 239000000463 material Substances 0.000 description 12
- 239000000243 solution Substances 0.000 description 11
- -1 polyethylene Polymers 0.000 description 9
- 239000004698 Polyethylene Substances 0.000 description 8
- 230000035699 permeability Effects 0.000 description 7
- 229920000573 polyethylene Polymers 0.000 description 7
- 238000010008 shearing Methods 0.000 description 7
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 6
- 239000012982 microporous membrane Substances 0.000 description 6
- 238000003825 pressing Methods 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 239000005662 Paraffin oil Substances 0.000 description 5
- 238000001816 cooling Methods 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000005191 phase separation Methods 0.000 description 4
- LCZVSXRMYJUNFX-UHFFFAOYSA-N 2-[2-(2-hydroxypropoxy)propoxy]propan-1-ol Chemical compound CC(O)COC(C)COC(C)CO LCZVSXRMYJUNFX-UHFFFAOYSA-N 0.000 description 3
- 239000004743 Polypropylene Substances 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 2
- 229920003235 aromatic polyamide Polymers 0.000 description 2
- 230000002457 bidirectional effect Effects 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 239000003085 diluting agent Substances 0.000 description 2
- 239000003292 glue Substances 0.000 description 2
- 238000007756 gravure coating Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000010998 test method Methods 0.000 description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 229920006310 Asahi-Kasei Polymers 0.000 description 1
- 229920013683 Celanese Polymers 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Natural products CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 1
- 230000005483 Hooke's law Effects 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- 239000006087 Silane Coupling Agent Substances 0.000 description 1
- 229920002125 Sokalan® Polymers 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 238000005524 ceramic coating Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000019441 ethanol Nutrition 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 description 1
- 229920000058 polyacrylate Polymers 0.000 description 1
- 239000004584 polyacrylic acid Substances 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- 239000011550 stock solution Substances 0.000 description 1
Images
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/489—Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C41/00—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
- B29C41/24—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of indefinite length
- B29C41/26—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of indefinite length by depositing flowable material on a rotating drum
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/07—Flat, e.g. panels
- B29C48/08—Flat, e.g. panels flexible, e.g. films
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
- B29C55/02—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
- B29C55/10—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial
- B29C55/12—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/403—Manufacturing processes of separators, membranes or diaphragms
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/403—Manufacturing processes of separators, membranes or diaphragms
- H01M50/406—Moulding; Embossing; Cutting
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/411—Organic material
- H01M50/414—Synthetic resins, e.g. thermoplastics or thermosetting resins
- H01M50/417—Polyolefins
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/446—Composite material consisting of a mixture of organic and inorganic materials
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/449—Separators, membranes or diaphragms characterised by the material having a layered structure
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/449—Separators, membranes or diaphragms characterised by the material having a layered structure
- H01M50/451—Separators, membranes or diaphragms characterised by the material having a layered structure comprising layers of only organic material and layers containing inorganic material
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/489—Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
- H01M50/491—Porosity
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/489—Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
- H01M50/494—Tensile strength
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Definitions
- the invention relates to the technical field of diaphragms, in particular to a diaphragm with high elastic deformation and a preparation method thereof.
- the diaphragm is crucial to the stability and safety of the battery.
- Elastic deformation is an important indicator for the stability of the diaphragm.
- the impact resistance of the diaphragm under stable physical properties can be judged by the size or presence of elastic deformation. After the diaphragm is changed, the elastic deformation rate is maintained to judge the damage degree of the change process.
- One of the objectives of the present invention is to provide a diaphragm with high elastic deformation to improve the stability of product properties, especially the stability of mechanical strength.
- the second object of the present invention is to provide a method for preparing a diaphragm with high elastic deformation, so as to prepare a diaphragm whose elastic deformation meets specific requirements.
- the third object of the present invention is to provide a lithium ion battery comprising the high elastic deformation diaphragm or the high elastic deformation diaphragm prepared by the preparation method.
- the present invention provides a diaphragm with high elastic deformation, which includes: a base film, or a base film and a coating on at least one side of the base film;
- the elastic deformation of the high elastic deformation diaphragm satisfies: ⁇ x/L>0.2%, preferably 0.8% ⁇ x/L ⁇ 10%, more preferably 1% ⁇ x/L ⁇ 5%;
- the present invention provides a method for preparing the high elastic deformation diaphragm, wherein the base film is prepared by a wet or dry process;
- the wet process includes the following steps:
- condition 1 and/or condition 2 the wet preparation process needs to meet condition 1 and/or condition 2:
- the solid content of polyolefin in the mixed slurry is less than 40%, the viscosity-average molecular weight of polyolefin (10,000)/drawing ratio>0.04, preferably>1, and the viscosity-average molecular weight of polyolefin (10,000)/MD stretching Ratio > 0.04; polyolefin viscosity-average molecular weight (10,000)/TD stretch ratio > 1, preferably > 10;
- Condition 2 the shrinkage step controls the shrinkage area ratio > 1%
- the dry process includes the following steps:
- the raw materials such as polyolefin resin and additives are pretreated according to the formula ratio, or directly transported to the extrusion system.
- the raw materials are melted and plasticized, and then the melt is extruded from the die to the casting roll to cool down, cooled and formed.
- Form a sheet (or base film) with a specific crystalline structure heat-treat the sheet to obtain a hard elastic film, then perform cold stretching and hot stretching, retract and shape to form a base film;
- condition 1' and/or condition 2' the dry preparation process needs to meet condition 1' and/or condition 2':
- Condition 1 viscosity-average molecular weight (10,000)/stretch ratio of polyolefin > 0.04, preferably > 1;
- Condition 2' the shrinkage step controls the shrinkage area ratio > 1%.
- the present invention provides a lithium ion battery, comprising the high elastic deformation separator or the high elastic deformation separator prepared by the preparation method.
- the invention prepares a diaphragm with a certain amount of elastic deformation by controlling raw materials and processing technology, ensures that the diaphragm maintains a certain elastic deformation rate after changes and during processing, improves the stability of product properties, especially the stability of mechanical strength, and makes the diaphragm
- the modified or assembled batteries have impact resistance under stable physical properties, thereby improving the stability and safety of lithium batteries.
- Fig. 1 is a flow chart of the preparation process of the high elastic deformation diaphragm provided by the embodiment of the present invention.
- a high elastic deformation diaphragm comprising: a base film, or, a base film and a coating placed on at least one side of the base film;
- the elastic deformation of the high elastic deformation diaphragm satisfies: ⁇ x/L>0.2%, such as 0.3%, 0.4%, 0.5%, 0.6%, 0.7%, 0.8%, 0.9%, 1%, 2%, 3% %, 4%, 5%, 6%, 7%, 8%, 9%, 10%, preferably 0.8% ⁇ x/L ⁇ 10%, more preferably 1% ⁇ x/L ⁇ 5%;
- the separator satisfying the above elastic deformation rate has good stability of physical properties, especially stability of mechanical strength, good impact resistance, and high stability and safety of the prepared lithium battery.
- the material of the base film is not particularly limited, and may be materials known in the art that can be used as the base film of a battery separator, including but not limited to polyethylene, polypropylene, polyethylene/polypropylene composite film, and the like.
- the material of the coating is not particularly limited, and may be materials known in the art that can be used as a coating on the diaphragm base film, including but not limited to inorganic materials (such as ceramics), organic polymers (such as aramid fiber, etc.), Inorganic/organic composite materials, etc.
- inorganic materials such as ceramics
- organic polymers such as aramid fiber, etc.
- Inorganic/organic composite materials etc.
- the thicknesses of the base film and the coating layer are not particularly limited as long as they are suitable for use as a separator of a battery.
- the thickness of the base film is 3-20 ⁇ m; the thickness of the single-side coating is 0.1-6 ⁇ m.
- a method for preparing a diaphragm with high elastic deformation including a wet process or a dry process.
- the wet process includes the following steps:
- condition 1 and/or condition 2 The wet preparation process needs to meet condition 1 and/or condition 2:
- the solid content of polyolefin in the mixed slurry (liquid hydrocarbon and polyolefin resin) is less than 40% (such as 35%, 30%, 25%), and the viscosity-average molecular weight of polyolefin (in tens of thousands)/stretch Ratio > 0.04, such as 0.05, 0.1, 0.2, 0.5, 0.8, 1.0, 2.0, 3.0, 5.0, 6.0, 7.0, 8.0, 10.0, preferably > 1, and the viscosity-average molecular weight of polyolefin (10,000)/MD draw ratio >0.04, such as 0.05, 0.1, 0.2, 0.5, 0.8, 1.0; polyolefin viscosity-average molecular weight (10,000)/TD draw ratio >1, such as 2.0, 3.0, 5.0, 6.0, 7.0, 8.0, 10.0, 12.0, 15.0, preferably>10;
- Stretching in the wet process is biaxial stretching, including longitudinal stretching and transverse stretching.
- the stretching ratio refers to the product of the longitudinal stretching ratio (ie, MD stretching ratio) and the transverse stretching ratio (ie, TD stretching ratio).
- MD or TD stretching ratio length after stretching/length before stretching.
- the shrinkage step controls the shrinkage area ratio > 1%, such as 2%, 3%, 5%;
- Retraction area ratio (area before retraction - area after retraction) / area before retraction
- the wet preparation process also needs to meet condition 3:
- Condition 3 Excluding the extrusion and stretching sections, other sections of the process control the longitudinal tension ⁇ 500N/m by adjusting the roller speed ratio or speed difference, such as 100, 150, 200, 250, 300, 400, 450N/m, through The holding force of the shearing roller or pressing roller controls the lateral tension of the diaphragm to ⁇ 100N/m, such as 10, 20, 50, 60, 80, 90N/m.
- Ways that can be implemented in the wet process include: condition 1, condition 2, condition 1+2, condition 1+3, condition 2+3, and condition 1+2+3.
- the dry process includes the following steps:
- the raw materials such as PE or PP and additives are pretreated according to the formula ratio, or directly transported to the extrusion system.
- the raw materials are melted and plasticized, and then extruded from the die to the casting roll to cool down, cooled and formed.
- a sheet (or base film) with a specific crystalline structure is formed, and the sheet is heat-treated to obtain a hard elastic film, followed by cold stretching and hot stretching to form a nano-microporous membrane, that is, a diaphragm.
- condition 1' and/or condition 2' the dry preparation process needs to meet condition 1' and/or condition 2':
- Condition 1' viscosity-average molecular weight (10,000)/stretch ratio of polyolefin > 0.04, such as 0.05, 0.1, 0.2, 0.5, 0.8, 1.0, 2.0, 3.0, 5.0, 6.0, 7.0, 8.0, 10.0, preferably > 1 ;
- the shrinkage setting step controls the shrinkage area ratio > 1%, such as 2%, 3%, 5%.
- the dry preparation process also needs to satisfy condition 3':
- Condition 3' Excluding the extrusion and stretching sections, the longitudinal tension of the other sections is controlled by the roller speed ratio or speed difference ⁇ 500N/m, such as 100, 150, 200, 250, 300, 400, 450N/m, The lateral tension of the diaphragm is controlled to be ⁇ 100N/m, such as 10, 20, 50, 60, 80, 90N/m, by the holding force of the shearing roller or the pressing roller.
- the ways that can be implemented in the dry process include: condition 1', condition 2', condition 1'+2', condition 1'+3', condition 2'+3', condition 1'+2'+3'.
- the preparation method also includes: a step of adding a coating on one side or both sides of the base film: the coating slurry is coated on the surface of the base film, dried or dried after treatment, and the coating slurry is formed by One or a combination of inorganic ceramic particles and organic polymer materials;
- the step of adding coating needs to meet condition 4:
- the inorganic ceramic particles are required to be 0.1 ⁇ m ⁇ D50 ⁇ 2.0 ⁇ m;
- the inorganic ceramic particles are required to be 0.01 ⁇ m ⁇ D50 ⁇ 4 ⁇ m;
- the D50 of the inorganic ceramic particles is required to be ⁇ 10 ⁇ m.
- the step of adding the coating also needs to meet condition 5: control the longitudinal tension ⁇ 150N/m during the coating, drying process or through the roller speed ratio or speed difference during the coating, treatment and drying process , such as 50, 100, 120N/m, the lateral tension is controlled to be less than 100N/m, such as 20, 50, 60, 80, 90N/m by the shearing or pressing roller holding force.
- the inorganic ceramic coating material in the coating slurry comprises the inorganic ceramic particles selected from alumina, boehmite, calcium carbonate, hydrotalcite, montmorillonite, spinel, mullite, titanium dioxide, di
- the inorganic ceramic particles selected from alumina, boehmite, calcium carbonate, hydrotalcite, montmorillonite, spinel, mullite, titanium dioxide, di
- the organic polymer material in the coating slurry contains organic coating materials such as polyimide, polyetherimide, aramid fiber, polysulfone fiber, polyvinylidene fluoride, polymethyl methacrylate, poly One or more of organic powders or suspensions such as ethylene oxide, polyacrylonitrile, polyvinylidene fluoride, polyvinylidene fluoride-hexafluoropropylene, etc.
- organic coating materials such as polyimide, polyetherimide, aramid fiber, polysulfone fiber, polyvinylidene fluoride, polymethyl methacrylate, poly One or more of organic powders or suspensions such as ethylene oxide, polyacrylonitrile, polyvinylidene fluoride, polyvinylidene fluoride-hexafluoropropylene, etc.
- the base film or base film + coating diaphragm prepared by the above method meets the requirement of ⁇ x/L>0.2%, which ensures that the diaphragm maintains a certain elastic deformation rate after changes and during processing, and improves the stability of product properties, especially
- the stability of mechanical strength enables the batteries modified or assembled with the diaphragm to have impact resistance under stable physical properties, thereby improving the stability and safety of lithium batteries.
- a lithium ion battery comprising the above-mentioned high elastic deformation separator or the high elastic deformation separator prepared by the above preparation method.
- Lithium-ion batteries have the same advantages as the above-mentioned separators, so I won't repeat them here.
- the raw materials, reagents, and methods used in the examples are conventional raw materials, reagents, and methods in the art.
- the diluent in this embodiment is paraffin oil
- the polyolefin resin in this embodiment is polyethylene with an average molecular weight of 900,000 (manufacturer: AsahiKASEI, model: UH650), and the equipment used is a wet-process diaphragm line from Sinoma Lithium Membrane Co., Ltd.
- a diaphragm with high elastic deformation and a preparation method thereof comprising mixing 75% by mass of paraffin oil and 25% by mass of polyethylene with an average molecular weight of 900,000, heating and melting to form a uniform mixture, and then cooling down Phase separation to obtain a membrane, and then heating the membrane to a temperature close to the melting point, and performing bidirectional simultaneous stretching (MD stretching 9 times, TD stretching 7 times) with a stretching ratio of 63 for the first time to orient the molecular chains, Then keep it warm for 3-15s, elute the residual liquid hydrocarbon with dichloromethane, a volatile solvent, and then dry it.
- MD stretching 9 times, TD stretching 7 times with a stretching ratio of 63 for the first time to orient the molecular chains
- the speed difference between the front and rear rollers is controlled to be less than 0.2m/min, so that the maximum value of the tension in the longitudinal process is ⁇ 300N/m, and the maximum value of the transverse tension of the diaphragm is controlled by the shearing roller or pressure roller to ⁇ 90N/m, and the interpenetrating and Microporous membrane material with high elastic deformation.
- the elastic deformation of the obtained diaphragm satisfies ⁇ x/L>1.2%, a thickness of 9 ⁇ m, a porosity of 40%, and an air permeability of 140 sec/100c.
- the diluent in this embodiment is paraffin oil
- the polyolefin resin in this embodiment is polyethylene (manufacturer: Celanese, model: GURX223) with an average molecular weight of 1.5 million
- the equipment used is a wet-process diaphragm line from Sinoma Lithium Membrane Co., Ltd.
- a diaphragm with high elastic deformation and a preparation method thereof comprising mixing 82% paraffin oil with a mass proportion of 18% and polyethylene with an average molecular weight of 1.5 million, heating and melting to form a uniform mixture, and then cooling down Phase separation to obtain a membrane, and then heating the membrane to a temperature close to the melting point, and performing bidirectional simultaneous stretching (7 times MD stretching, 7 times TD stretching) with a stretching ratio of 49 for the first time to orient the molecular chains, followeded by heat preservation for a certain period of time, the residual liquid hydrocarbons were eluted with volatile solvent dichloromethane, then dried, and finally through the second transverse stretching (TD stretching ratio 1.4 times), the area retracted by 18% after setting, the whole process
- the speed difference between the front and rear rollers to be less than 0.3m/min
- the maximum value of the tension in the longitudinal process is ⁇ 400N/m
- the maximum value of the transverse tension of the diaphragm is controlled by the shearing roller or
- paraffin oil accounts for 80%
- polyethylene accounts for 20%
- TD stretching ratio is 1.45 times
- the elastic deformation of the obtained diaphragm satisfies ⁇ x/L>1.3%, a thickness of 12 ⁇ m, a porosity of 40%, and an air permeability of 155 sec/100c.
- the 3-20 ⁇ m diaphragm (base film) can be prepared through the process conditions of Examples 1-3, the elastic deformation of the diaphragm satisfies ⁇ x/L>0.8%, the porosity is 25-70%, and the air permeability value is 50-400sec/ 100c.
- a diaphragm with high elastic deformation and its preparation method The composition and content of the coating are: 92 parts of alumina with a D50 of 0.6 ⁇ m, 4.5 parts of modified polyacrylic acid, 2.5 parts of polyvinyl alcohol, and 1 part of ammonium polyacrylate.
- Stir to prepare a water-based coating slurry with a solid content of 30% use the 9 ⁇ m prepared in Example 1 as the base film, and use the MCD type coater to gravure-coat the combined slurry of the above-mentioned water-based coating on the base film sheet. side, and finally after being baked in an oven, the coating thickness is 3 ⁇ m.
- the speed difference between the front and rear rollers is controlled to be less than 0.2m/min during the whole process, so that the maximum tension in the longitudinal process is less than 100N/m.
- the maximum value of the transverse tension is controlled by force ⁇ 50N/m, and the microporous membrane material with interpenetration and high elastic deformation is prepared.
- the elastic deformation of the obtained diaphragm satisfies ⁇ x/L>0.5%, the thickness is 12 ⁇ m, and the air permeability is 170 sec/100c.
- a high elastic deformation diaphragm and a preparation method thereof 15 parts by weight of polyvinylidene fluoride glue solution (20% by mass fraction) and 20 parts by weight of polyimide glue solution (10% by mass fraction), are dissolved to 57 In the mixed liquid of dimethylacetamide and tripropylene glycol (wherein, the weight ratio of dimethylacetamide, tripropylene glycol and water is 15:70:30), add 20 parts by weight of silane coupling agent modified D50 is 0.64 ⁇ m alumina, 3 parts by weight of emulsion-type acrylate binder (solid content is 40%, viscosity is 20cps-200cps at 25°C), mixed and stirred at room temperature for 1 hour to obtain a white viscous coating slurry.
- Example 2 The 7 ⁇ m prepared in Example 2 is used as the base film, and the above-mentioned coating slurry is coated on one side of the base film by means of gravure coating by an MCD type coater, and then immersed in a coagulation solution (dimethyl ethyl alcohol) at 22 ° C.
- a coagulation solution dimethyl ethyl alcohol
- the weight ratio of amide, tripropylene glycol and water is 28:12:60), and the wet film on the surface of the polyolefin porous membrane is first cured, washed with water and dried in turn to obtain a composite diaphragm.
- the thickness is 2 ⁇ m, and the speed difference between the front and rear rollers is controlled to be less than 0.1m/min in the whole process, so that the maximum tension in the longitudinal process is ⁇ 120N/m, and the maximum tension in the transverse direction is controlled by the shearing roller or pressing roller to ⁇ 60N/m.
- a diaphragm with high elastic deformation and its preparation method dispersing alumina powder with 0.1 times the mass of aramid fiber and D50 of 0.8 ⁇ m in the aramid fiber stock solution with a mass fraction of 1.5% and an apparent viscosity of 300cp, and passing it through a high-speed dispersing emulsifier Stir for 30 minutes, and obtain a uniform para-aramid slurry after filtering through a 1000-mesh filter.
- the 12 ⁇ m prepared in Example 3 is used as the base film, and the above-mentioned para-aramid slurry is coated on one side of the base film by means of gravure coating through an MCD type coating machine.
- the speed difference between the front and rear rollers is controlled to be less than 0.15m/min, so that the maximum tension in the longitudinal process is less than 110N/m, and the maximum tension in the transverse direction is less than 80N/m through the holding force of the shearing roller or pressing roller.
- Microporous membrane material with elastic deformation The elastic deformation of the obtained diaphragm satisfies ⁇ x/L>0.8%, the thickness is 16 ⁇ m, and the air permeability is 260 sec/100c.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Inorganic Chemistry (AREA)
- Materials Engineering (AREA)
- Composite Materials (AREA)
- Cell Separators (AREA)
Abstract
The present invention relates to the technical field of separators. Provided are a separator having a large elastic deformation quantity and a preparation method therefor. The separator having a large elastic deformation quantity comprises: a base film, or a base film and a coating applied on at least one side of the base film; and the elastic deformation quantity of the separator having a large elastic deformation quantity satisfies: Δx/L > 0.2%. By means of the present invention, the technical problem of irreversible damage occurring in separator processing and modification processes is solved, and the technical effects of improving the physical property stability, especially the mechanical strength stability, of a product, enabling a battery cell having a modified separator or assembled using the separator to have an impact resistance capability under a stable physical property, and thereby improving the stability and safety of a lithium battery are achieved.
Description
本发明涉及隔膜技术领域,尤其是涉及一种高弹性形变量隔膜及其制备方法。The invention relates to the technical field of diaphragms, in particular to a diaphragm with high elastic deformation and a preparation method thereof.
隔膜作为锂离子电池体系中关键主材,对电池的各项性能稳定性、安全性能至关重要。As the key main material in the lithium-ion battery system, the diaphragm is crucial to the stability and safety of the battery.
现有技术主要通过无机、有机或无机有机混涂、改性提高隔膜耐热性、降低闭孔温度,以提高电池的稳定性、安全性。公开号为JP6069677B2通过有机、无机混涂提升隔膜的耐热性,公开号为CN104185551B通过涂层改性降低隔膜的闭孔温度来提高电池的安全性。In the prior art, mainly through inorganic, organic or inorganic-organic mixed coating and modification, the heat resistance of the diaphragm is improved, and the closed cell temperature is reduced, so as to improve the stability and safety of the battery. The publication number is JP6069677B2, which improves the heat resistance of the separator through organic and inorganic mixed coating, and the publication number is CN104185551B, which improves the safety of the battery by reducing the closed cell temperature of the separator through coating modification.
对于形变,目前主要关注断裂伸长率,对于弹性形变很少关注,弹性形变是隔膜保持物性稳定的一个重要指标,通过弹性形变大小或者有无可以判断隔膜在物性稳定下的耐冲击能力,通过隔膜发生改变后保持弹性形变率以判断改变过程的损伤程度。For deformation, at present, the main focus is on the elongation at break, and little attention is paid to elastic deformation. Elastic deformation is an important indicator for the stability of the diaphragm. The impact resistance of the diaphragm under stable physical properties can be judged by the size or presence of elastic deformation. After the diaphragm is changed, the elastic deformation rate is maintained to judge the damage degree of the change process.
有鉴于此,特提出本发明。In view of this, the present invention is proposed.
发明内容Contents of the invention
本发明的目的之一在于提供一种高弹性形变量隔膜,提高产品物性稳定性尤其是力学强度稳定性。One of the objectives of the present invention is to provide a diaphragm with high elastic deformation to improve the stability of product properties, especially the stability of mechanical strength.
本发明的目的之二在于提供一种高弹性形变量隔膜的制备方法,制备出弹性形变满足特定要求的隔膜。The second object of the present invention is to provide a method for preparing a diaphragm with high elastic deformation, so as to prepare a diaphragm whose elastic deformation meets specific requirements.
本发明的目的之三在于提供一种包括所述高弹性形变量隔膜或所述制备方法制备得到的高弹性形变量隔膜的锂离子电池。The third object of the present invention is to provide a lithium ion battery comprising the high elastic deformation diaphragm or the high elastic deformation diaphragm prepared by the preparation method.
为了实现本发明的上述目的,特采用以下技术方案:In order to realize the above-mentioned purpose of the present invention, special adopt following technical scheme:
第一方面,本发明提供了一种高弹性形变量隔膜,所述高弹性形变量隔膜包括:基膜,或,基膜与置于基膜至少一面上的涂层;In a first aspect, the present invention provides a diaphragm with high elastic deformation, which includes: a base film, or a base film and a coating on at least one side of the base film;
所述高弹性形变量隔膜的弹性形变量满足:Δx/L>0.2%,优选0.8%<Δx/L<10%,进一步优选1%<Δx/L<5%;The elastic deformation of the high elastic deformation diaphragm satisfies: Δx/L>0.2%, preferably 0.8%<Δx/L<10%, more preferably 1%<Δx/L<5%;
其中,L为原始长度,单位:米;Δx为弹性形变量,单位:米。Among them, L is the original length, unit: meter; Δx is the elastic deformation, unit: meter.
第二方面,本发明提供了一种所述高弹性形变量隔膜的制备方法,所述基膜采用湿法或干法工艺制备;In a second aspect, the present invention provides a method for preparing the high elastic deformation diaphragm, wherein the base film is prepared by a wet or dry process;
湿法工艺包括以下步骤:The wet process includes the following steps:
将液态烃与聚烯烃树脂混合按照配方比例预处理,或直接输送至挤出系统,加热熔融形成均匀的混合物;混合熔体挤出至流延辊降温,进行相分离,冷却成型,制得膜片;再将膜片加热至接近熔点温度,进行双向同步或者分步拉伸使分子链取向,保温、定型;溶剂洗脱残留的液态烃,洗脱后将膜移出溶剂,干燥,然后再横向拉伸、定型、回缩,制备出相互贯通的微孔膜;Mix liquid hydrocarbons and polyolefin resins for pretreatment according to the formula ratio, or directly transport them to the extrusion system, heat and melt to form a uniform mixture; the mixed melt is extruded to the casting roll to cool down, phase separation, cooling and molding, and the film is obtained Then heat the membrane to a temperature close to the melting point, carry out two-way synchronous or step-by-step stretching to make the molecular chain orientation, heat preservation, and finalization; the solvent elutes the residual liquid hydrocarbons, and after elution, the membrane is removed from the solvent, dried, and then horizontally Stretching, shaping, and retraction to prepare interpenetrating microporous membranes;
其中,湿法制备过程需满足条件1和/或条件2:Among them, the wet preparation process needs to meet condition 1 and/or condition 2:
条件1:混合浆料中聚烯烃的固含量<40%,聚烯烃的粘均分子量(万)/拉伸倍率>0.04,优选>1,且聚烯烃的粘均分子量(万)/MD拉伸倍率>0.04;聚烯烃的粘均分子量(万)/TD拉伸倍率>1,优选>10;Condition 1: The solid content of polyolefin in the mixed slurry is less than 40%, the viscosity-average molecular weight of polyolefin (10,000)/drawing ratio>0.04, preferably>1, and the viscosity-average molecular weight of polyolefin (10,000)/MD stretching Ratio > 0.04; polyolefin viscosity-average molecular weight (10,000)/TD stretch ratio > 1, preferably > 10;
条件2:回缩步骤控制回缩面积比例>1%;Condition 2: the shrinkage step controls the shrinkage area ratio > 1%;
或,干法工艺包括以下步骤:Alternatively, the dry process includes the following steps:
将聚烯烃树脂及添加剂等原料按照配方比例预处理,或直接输送至挤出系统,原料在挤出系统中,经熔融塑化后从模头挤出熔体至流延辊降温,冷却成型,形成特定结晶结构的片材(或基膜),将片材进行热处理后得到硬弹性薄膜,随后进行冷拉伸和热拉伸后,回缩、定型形成基膜;The raw materials such as polyolefin resin and additives are pretreated according to the formula ratio, or directly transported to the extrusion system. In the extrusion system, the raw materials are melted and plasticized, and then the melt is extruded from the die to the casting roll to cool down, cooled and formed. Form a sheet (or base film) with a specific crystalline structure, heat-treat the sheet to obtain a hard elastic film, then perform cold stretching and hot stretching, retract and shape to form a base film;
其中,干法制备过程需满足条件1’和/或条件2’:Among them, the dry preparation process needs to meet condition 1' and/or condition 2':
条件1’:聚烯烃的粘均分子量(万)/拉伸倍率>0.04,优选>1;Condition 1': viscosity-average molecular weight (10,000)/stretch ratio of polyolefin > 0.04, preferably > 1;
条件2’:回缩步骤控制回缩面积比例>1%。Condition 2': the shrinkage step controls the shrinkage area ratio > 1%.
第三方面,本发明提供了一种锂离子电池,包括所述高弹性形变量隔膜或所述制备方法制备得到的高弹性形变量隔膜。In a third aspect, the present invention provides a lithium ion battery, comprising the high elastic deformation separator or the high elastic deformation separator prepared by the preparation method.
本发明的技术方案具有如下有益效果:The technical solution of the present invention has the following beneficial effects:
本发明通过控制原材料及加工工艺制备具有一定的弹性形变量的隔膜,保证隔膜在发生改变后以及在加工过程中保持一定的弹性形变率,提高产品物性稳定性尤其是力学强度稳定性,使隔膜改性或组装的电芯具备在物性稳定下的耐冲击能力,进而提高锂电池稳定性、安全性。The invention prepares a diaphragm with a certain amount of elastic deformation by controlling raw materials and processing technology, ensures that the diaphragm maintains a certain elastic deformation rate after changes and during processing, improves the stability of product properties, especially the stability of mechanical strength, and makes the diaphragm The modified or assembled batteries have impact resistance under stable physical properties, thereby improving the stability and safety of lithium batteries.
为了更清楚地说明本发明具体实施方式或现有技术中的技术方案,下面将对具体实施方式或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图是本发明的一些实施方式,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the specific implementation of the present invention or the technical solutions in the prior art, the following will briefly introduce the accompanying drawings that need to be used in the specific implementation or description of the prior art. Obviously, the accompanying drawings in the following description The drawings show some implementations of the present invention, and those skilled in the art can obtain other drawings based on these drawings without any creative effort.
图1为本发明实施例提供的高弹性形变量隔膜的制备过程流程图。Fig. 1 is a flow chart of the preparation process of the high elastic deformation diaphragm provided by the embodiment of the present invention.
下面将结合实施例对本发明的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions of the present invention will be clearly and completely described below in conjunction with the embodiments. Obviously, the described embodiments are part of the embodiments of the present invention, but not all of them. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.
根据本发明的第一个方面,提供了一种高弹性形变量隔膜,包括:基膜,或,基膜与置于基膜至少一面上的涂层;According to a first aspect of the present invention, a high elastic deformation diaphragm is provided, comprising: a base film, or, a base film and a coating placed on at least one side of the base film;
所述高弹性形变量隔膜的弹性形变量满足:Δx/L>0.2%,例如为0.3%、0.4%、0.5%、0.6%、0.7%、0.8%、0.9%、1%、2%、3%、4%、5%、6%、7%、8%、9%、10%,优选0.8%<Δx/L<10%,进一步优选1%<Δx/L<5%;The elastic deformation of the high elastic deformation diaphragm satisfies: Δx/L>0.2%, such as 0.3%, 0.4%, 0.5%, 0.6%, 0.7%, 0.8%, 0.9%, 1%, 2%, 3% %, 4%, 5%, 6%, 7%, 8%, 9%, 10%, preferably 0.8%<Δx/L<10%, more preferably 1%<Δx/L<5%;
其中,L为原始长度,单位:米;Δx为弹性形变量,单位:米。Among them, L is the original length, unit: meter; Δx is the elastic deformation, unit: meter.
弹性形变测试方法按照GB/1040.3-2006规定测试拉伸强度、断裂伸长率的测试方法,根据胡克定律(弹性定律):F=k·Δx(其中F是弹力,单位是N,k是常数,是物体的劲度(倔强)系数,单位是N/m,Δx是形变量,单位是m),判断弹性形变量。Elastic deformation test method According to the test method of GB/1040.3-2006 to test tensile strength and elongation at break, according to Hooke's law (elastic law): F=k·Δx (where F is elastic force, the unit is N, k is The constant is the stiffness (stiffness) coefficient of the object, the unit is N/m, Δx is the deformation amount, the unit is m), and the elastic deformation amount is judged.
满足上述弹性形变率的隔膜具有较好的物性稳定性尤其是力学强度稳定性,耐冲击能力好,制备成锂电池稳定性和安全性高。The separator satisfying the above elastic deformation rate has good stability of physical properties, especially stability of mechanical strength, good impact resistance, and high stability and safety of the prepared lithium battery.
对基膜的材料没有特别的限定,可以为本领域已知的可用作电池隔膜基膜的材料,包括但不限于聚乙烯、聚丙烯、聚乙烯/聚丙烯复合膜等。The material of the base film is not particularly limited, and may be materials known in the art that can be used as the base film of a battery separator, including but not limited to polyethylene, polypropylene, polyethylene/polypropylene composite film, and the like.
对涂层的材料没有特别的限定,可以为本领域已知的可用作隔膜基膜上涂覆的材料,包括但不限于无机材料(例如陶瓷)、有机聚合物(例如芳纶等)、无机/有机复合材料等。The material of the coating is not particularly limited, and may be materials known in the art that can be used as a coating on the diaphragm base film, including but not limited to inorganic materials (such as ceramics), organic polymers (such as aramid fiber, etc.), Inorganic/organic composite materials, etc.
对基膜和涂层的厚度没有特别限定,只要其适合用作电池的隔膜即可。优选地,基膜厚度为3~20μm;单面涂层厚度为0.1~6μm。The thicknesses of the base film and the coating layer are not particularly limited as long as they are suitable for use as a separator of a battery. Preferably, the thickness of the base film is 3-20 μm; the thickness of the single-side coating is 0.1-6 μm.
根据本发明的第二个方面,提供了一种高弹性形变量隔膜的制备方法,如图1所示,包括湿法工艺或干法工艺。According to the second aspect of the present invention, there is provided a method for preparing a diaphragm with high elastic deformation, as shown in FIG. 1 , including a wet process or a dry process.
湿法工艺包括以下步骤:The wet process includes the following steps:
将液态烃与聚烯烃树脂混合按照配方比例预处理,或直接输送至挤出系统,加热熔融形成均匀的混合物;混合熔体挤出至流延辊降温,进行相分离,冷却成型,制得膜片;再将膜片加热至接近熔点温度,进行双向同步或者分步拉伸使分子链取向,保温、定型;溶剂洗脱残留的液态烃,洗脱后将膜移出溶剂,干燥,然后再横向拉伸、定型、回缩,制备出相互贯通的微孔膜。Mix liquid hydrocarbons and polyolefin resins for pretreatment according to the formula ratio, or directly transport them to the extrusion system, heat and melt to form a uniform mixture; the mixed melt is extruded to the casting roll to cool down, phase separation, cooling and molding, and the film is obtained Then heat the membrane to a temperature close to the melting point, carry out two-way synchronous or step-by-step stretching to make the molecular chain orientation, heat preservation, and finalization; the solvent elutes the residual liquid hydrocarbons, and after elution, the membrane is removed from the solvent, dried, and then horizontally Stretching, shaping, and retraction to prepare interpenetrating microporous membranes.
湿法制备过程需满足条件1和/或条件2:The wet preparation process needs to meet condition 1 and/or condition 2:
条件1:混合浆料(液态烃与聚烯烃树脂)中聚烯烃的固含量<40%(例如35%、30%、25%),聚烯烃的粘均分子量(以万为单位)/拉伸倍率>0.04,例如0.05、0.1、0.2、0.5、0.8、1.0、2.0、3.0、5.0、6.0、7.0、8.0、10.0,优选>1,且聚烯烃的粘均分子量(万)/MD拉伸倍率>0.04,例如0.05、0.1、0.2、0.5、0.8、1.0;聚烯烃的粘均分子量(万)/TD拉伸倍率>1,例如2.0、3.0、5.0、6.0、7.0、8.0、10.0、12.0、15.0,优选>10;Condition 1: The solid content of polyolefin in the mixed slurry (liquid hydrocarbon and polyolefin resin) is less than 40% (such as 35%, 30%, 25%), and the viscosity-average molecular weight of polyolefin (in tens of thousands)/stretch Ratio > 0.04, such as 0.05, 0.1, 0.2, 0.5, 0.8, 1.0, 2.0, 3.0, 5.0, 6.0, 7.0, 8.0, 10.0, preferably > 1, and the viscosity-average molecular weight of polyolefin (10,000)/MD draw ratio >0.04, such as 0.05, 0.1, 0.2, 0.5, 0.8, 1.0; polyolefin viscosity-average molecular weight (10,000)/TD draw ratio >1, such as 2.0, 3.0, 5.0, 6.0, 7.0, 8.0, 10.0, 12.0, 15.0, preferably>10;
湿法工艺中拉伸是双向拉伸,包括纵向拉伸和横向拉伸,拉伸倍率指纵拉伸倍率(即MD拉伸倍率)与横向拉伸倍率(即TD拉伸倍率)之乘积。Stretching in the wet process is biaxial stretching, including longitudinal stretching and transverse stretching. The stretching ratio refers to the product of the longitudinal stretching ratio (ie, MD stretching ratio) and the transverse stretching ratio (ie, TD stretching ratio).
MD或TD拉伸倍率=拉伸后长度/拉伸前长度。MD or TD stretching ratio=length after stretching/length before stretching.
条件2:回缩步骤控制回缩面积比例>1%,例如2%、3%、5%;Condition 2: the shrinkage step controls the shrinkage area ratio > 1%, such as 2%, 3%, 5%;
回缩面积比例=(回缩前面积-回缩后面积)/回缩前面积Retraction area ratio = (area before retraction - area after retraction) / area before retraction
在一种优选的实施方式中,湿法制备过程还需要满足条件3:In a preferred embodiment, the wet preparation process also needs to meet condition 3:
条件3:除去挤出、拉伸段,其它段工艺过程通过调节辊筒速比或速差控制纵向张力<500N/m,例如100、150、200、250、300、400、450N/m,通过剪辊或压辊加持力控制隔膜横向张力<100N/m,例如10、20、50、60、80、90N/m。Condition 3: Excluding the extrusion and stretching sections, other sections of the process control the longitudinal tension <500N/m by adjusting the roller speed ratio or speed difference, such as 100, 150, 200, 250, 300, 400, 450N/m, through The holding force of the shearing roller or pressing roller controls the lateral tension of the diaphragm to <100N/m, such as 10, 20, 50, 60, 80, 90N/m.
在湿法工艺中可实施的方式包括:条件1、条件2、条件1+2、条件1+3、条件2+3、条件1+2+3。Ways that can be implemented in the wet process include: condition 1, condition 2, condition 1+2, condition 1+3, condition 2+3, and condition 1+2+3.
干法工艺包括以下步骤:The dry process includes the following steps:
将PE或PP及添加剂等原料按照配方比例预处理,或直接输送至挤出系统,原料在挤出系统中,经熔融塑化后从模头挤出熔体至流延辊降温,冷却成型,形成特定结晶结构的片材(或基膜),将片材进行热处理后得到硬弹性薄膜,随后进行冷拉伸和热拉伸后形成纳米微孔膜,即隔膜。The raw materials such as PE or PP and additives are pretreated according to the formula ratio, or directly transported to the extrusion system. In the extrusion system, the raw materials are melted and plasticized, and then extruded from the die to the casting roll to cool down, cooled and formed. A sheet (or base film) with a specific crystalline structure is formed, and the sheet is heat-treated to obtain a hard elastic film, followed by cold stretching and hot stretching to form a nano-microporous membrane, that is, a diaphragm.
其中,干法制备过程需满足条件1’和/或条件2’:Among them, the dry preparation process needs to meet condition 1' and/or condition 2':
条件1’:聚烯烃的粘均分子量(万)/拉伸倍率>0.04,例如0.05、0.1、0.2、0.5、0.8、1.0、2.0、3.0、5.0、6.0、7.0、8.0、10.0,优选>1;Condition 1': viscosity-average molecular weight (10,000)/stretch ratio of polyolefin > 0.04, such as 0.05, 0.1, 0.2, 0.5, 0.8, 1.0, 2.0, 3.0, 5.0, 6.0, 7.0, 8.0, 10.0, preferably > 1 ;
干法工艺中只有单向拉伸,拉伸倍率就指单向的拉伸倍率。There is only unidirectional stretching in the dry process, and the stretching ratio refers to the unidirectional stretching ratio.
条件2’:回缩定型步骤控制回缩面积比例>1%,例如2%、3%、5%。Condition 2': the shrinkage setting step controls the shrinkage area ratio > 1%, such as 2%, 3%, 5%.
在一种优选的实施方式中,干法制备过程还需要满足条件3’:In a preferred embodiment, the dry preparation process also needs to satisfy condition 3':
条件3’:除去挤出、拉伸段,其它段的工艺过程通过辊筒速比或速差控制纵向张力<500N/m,例如100、150、200、250、300、400、450N/m,通过剪辊或压辊加持力控制隔膜横向张力<100N/m,例如10、20、50、60、80、90N/m。Condition 3': Excluding the extrusion and stretching sections, the longitudinal tension of the other sections is controlled by the roller speed ratio or speed difference <500N/m, such as 100, 150, 200, 250, 300, 400, 450N/m, The lateral tension of the diaphragm is controlled to be <100N/m, such as 10, 20, 50, 60, 80, 90N/m, by the holding force of the shearing roller or the pressing roller.
在干法工艺中可实施的方式包括:条件1’、条件2’、条件1’+2’、条件1’+3’、条件2’+3’、条件1’+2’+3’。The ways that can be implemented in the dry process include: condition 1', condition 2', condition 1'+2', condition 1'+3', condition 2'+3', condition 1'+2'+3'.
作为进一步的方案,所述制备方法还包括:在基膜单侧或两侧增加涂层的步骤:涂覆浆料涂覆在基膜表面,经过干燥或处理后干燥形成,涂覆浆料由无机陶瓷颗粒、有机聚合物材料中的一种或混合组成;As a further solution, the preparation method also includes: a step of adding a coating on one side or both sides of the base film: the coating slurry is coated on the surface of the base film, dried or dried after treatment, and the coating slurry is formed by One or a combination of inorganic ceramic particles and organic polymer materials;
其中,增加涂层的步骤需要满足条件4:Among them, the step of adding coating needs to meet condition 4:
当无机陶瓷颗粒的重量占比>80%时(例如85%、90%、95%),要求无机陶瓷颗粒0.1μm≤D50≤2.0μm;When the weight ratio of inorganic ceramic particles is >80% (such as 85%, 90%, 95%), the inorganic ceramic particles are required to be 0.1μm≤D50≤2.0μm;
当无机陶瓷颗粒的重量占比在30%-80%时(例如40%、50%、60%、70%),要求无机陶瓷颗粒0.01μm≤D50≤4μm;When the weight ratio of inorganic ceramic particles is 30%-80% (such as 40%, 50%, 60%, 70%), the inorganic ceramic particles are required to be 0.01μm≤D50≤4μm;
当无机陶瓷颗粒的重量占比<30%时(例如5%、10%、20%),要求无机陶瓷颗粒D50≤10μm。When the weight ratio of the inorganic ceramic particles is less than 30% (for example, 5%, 10%, 20%), the D50 of the inorganic ceramic particles is required to be ≤ 10 μm.
在一种优选的实施方式中,增加涂层的步骤还需要满足条件5:在涂覆、干燥过程或在涂覆、处理、干燥过程通过辊筒速比或速差控制纵向张力<150N/m,例如50、100、120N/m,通过剪辊或压辊加持力控制横向张力小于100N/m,例如20、50、60、80、90N/m。In a preferred embodiment, the step of adding the coating also needs to meet condition 5: control the longitudinal tension <150N/m during the coating, drying process or through the roller speed ratio or speed difference during the coating, treatment and drying process , such as 50, 100, 120N/m, the lateral tension is controlled to be less than 100N/m, such as 20, 50, 60, 80, 90N/m by the shearing or pressing roller holding force.
在增加涂层的步骤中可实施的方式包括:条件4或条件4+5。The ways that can be implemented in the step of adding the coating include: condition 4 or condition 4+5.
优选地,涂覆浆料中无机陶瓷涂覆材料包含包括所述无机陶瓷颗粒选自氧化铝、勃姆石、碳酸钙、水滑石、蒙脱土、尖晶石、莫来石、二氧化钛、二氧化硅、二氧化锆、氧化镁、氧化钙、氧化铍、氢氧化镁、氮化硼、氮化硅、氮化铝、氮化钛、碳化硼、碳化硅、碳化锆中的一种或几种;Preferably, the inorganic ceramic coating material in the coating slurry comprises the inorganic ceramic particles selected from alumina, boehmite, calcium carbonate, hydrotalcite, montmorillonite, spinel, mullite, titanium dioxide, di One or more of silicon oxide, zirconium dioxide, magnesium oxide, calcium oxide, beryllium oxide, magnesium hydroxide, boron nitride, silicon nitride, aluminum nitride, titanium nitride, boron carbide, silicon carbide, zirconium carbide kind;
优选地,涂覆浆料中有机聚合物材料包含有机涂覆材料为聚酰亚胺、聚醚酰亚胺、芳纶、芳砜纶、聚偏二氟乙烯、聚甲基丙烯酸甲酯、聚环氧乙烷、聚丙烯腈、聚偏氟乙烯、聚偏氟乙烯-六氟丙烯等有机粉料或悬浮液中的一种或两种以上。Preferably, the organic polymer material in the coating slurry contains organic coating materials such as polyimide, polyetherimide, aramid fiber, polysulfone fiber, polyvinylidene fluoride, polymethyl methacrylate, poly One or more of organic powders or suspensions such as ethylene oxide, polyacrylonitrile, polyvinylidene fluoride, polyvinylidene fluoride-hexafluoropropylene, etc.
采用上述方法制备得到的基膜或基膜+涂层隔膜满足Δx/L>0.2%的要求,保证隔膜在发生改变后以及在加工过程中保持一定的弹性形变率,提高产品物性稳定性尤其是力学强度稳定性,使隔膜改性或组装的电芯具备在物性稳定下的耐冲击能力,进而提高锂电池稳定性、安全性。The base film or base film + coating diaphragm prepared by the above method meets the requirement of Δx/L>0.2%, which ensures that the diaphragm maintains a certain elastic deformation rate after changes and during processing, and improves the stability of product properties, especially The stability of mechanical strength enables the batteries modified or assembled with the diaphragm to have impact resistance under stable physical properties, thereby improving the stability and safety of lithium batteries.
根据本发明的第三个方面,提供了一种锂离子电池,包括上述高弹性形变量隔膜或上述制备方法制备得到的高弹性形变量隔膜。According to a third aspect of the present invention, a lithium ion battery is provided, comprising the above-mentioned high elastic deformation separator or the high elastic deformation separator prepared by the above preparation method.
锂离子电池具有与上述隔膜相同的优势,在此不再赘述。Lithium-ion batteries have the same advantages as the above-mentioned separators, so I won't repeat them here.
下面结合实施例对本发明作进一步的说明,需要说明的是,提供以下实施例仅出于说明目的并不构成对本发明要求保护范围的限制。The present invention will be further described below in conjunction with the examples. It should be noted that the following examples are provided only for the purpose of illustration and do not constitute a limitation to the protection scope of the present invention.
除特殊说明外,在实施例中所采用的原料、试剂、方法等均为本领域常规的原料、试剂、方法。Unless otherwise specified, the raw materials, reagents, and methods used in the examples are conventional raw materials, reagents, and methods in the art.
实施例1Example 1
本实施例稀释剂为石蜡油,本实施例聚烯烃树脂为分子量均值为90万的聚乙烯(厂家:AsahiKASEI,型号:UH650),所用设备为中材锂膜有限公司湿法隔膜线。The diluent in this embodiment is paraffin oil, the polyolefin resin in this embodiment is polyethylene with an average molecular weight of 900,000 (manufacturer: AsahiKASEI, model: UH650), and the equipment used is a wet-process diaphragm line from Sinoma Lithium Membrane Co., Ltd.
一种高弹性形变量隔膜及其制备方法,将质量占比为75%石蜡油与质量占比为25%、平均分子量90万的聚乙烯混合,加热熔融后,形成均匀的混合物,然后降温进行相分离,制得膜片,再将膜片加热至接近熔点温度,进行第一次拉伸倍率为63的双向同步拉伸(MD拉伸9倍、TD拉伸7倍)使分子链取向,紧接着保温3~15s,用易挥发溶剂二氯甲烷洗脱残留的液态烃,然后干燥,最后通过第二次横向拉伸(TD拉伸倍率1.5倍)、定型后面积回缩15%,整个过程通过临近前后辊筒速度差控制小于0.2m/min,使得纵向过程张力最大值<300N/m,通过剪辊或压辊加持力控制隔膜横向张力最大值<90N/m,制备出相互贯通且高弹性形变量的微孔膜材料。所得隔膜弹性形变量满足Δx/L>1.2%、厚度9μm、孔隙率40%、透气度值为140sec/100c。A diaphragm with high elastic deformation and a preparation method thereof, comprising mixing 75% by mass of paraffin oil and 25% by mass of polyethylene with an average molecular weight of 900,000, heating and melting to form a uniform mixture, and then cooling down Phase separation to obtain a membrane, and then heating the membrane to a temperature close to the melting point, and performing bidirectional simultaneous stretching (MD stretching 9 times, TD stretching 7 times) with a stretching ratio of 63 for the first time to orient the molecular chains, Then keep it warm for 3-15s, elute the residual liquid hydrocarbon with dichloromethane, a volatile solvent, and then dry it. Finally, after the second transverse stretching (TD stretching ratio 1.5 times), the area shrinks by 15% after setting, and the whole In the process, the speed difference between the front and rear rollers is controlled to be less than 0.2m/min, so that the maximum value of the tension in the longitudinal process is <300N/m, and the maximum value of the transverse tension of the diaphragm is controlled by the shearing roller or pressure roller to <90N/m, and the interpenetrating and Microporous membrane material with high elastic deformation. The elastic deformation of the obtained diaphragm satisfies Δx/L>1.2%, a thickness of 9 μm, a porosity of 40%, and an air permeability of 140 sec/100c.
实施例2Example 2
本实施例稀释剂为石蜡油,本实施例聚烯烃树脂为分子量均值为150万的聚乙烯(厂家:Celanese,型号:GURX223),所用设备为中材锂膜有限公司湿法隔膜线。The diluent in this embodiment is paraffin oil, the polyolefin resin in this embodiment is polyethylene (manufacturer: Celanese, model: GURX223) with an average molecular weight of 1.5 million, and the equipment used is a wet-process diaphragm line from Sinoma Lithium Membrane Co., Ltd.
一种高弹性形变量隔膜及其制备方法,将质量占比为82%石蜡油与质量占比为18%、平均分子量150万的聚乙烯混合,加热熔融后,形成均匀的混合物,然后降温进行相分离,制得膜片,再将膜片加热至接近熔点温度,进行第一次拉伸倍率为49的双向同步拉伸(MD拉伸7倍、TD拉伸7倍)使分子链取向,紧接着保温一定时间,用易挥发溶剂二氯甲烷洗脱残留的液态烃,然后干燥,最后通过第二次横向拉伸(TD拉伸倍率1.4倍)、定型后面积回缩18%,整个过程通过临近前后辊筒速度差控制小于0.3m/min, 使得纵向过程张力最大值<400N/m,通过剪辊或压辊加持力控制隔膜横向张力最大值<100N/m,制备出相互贯通且高弹性形变量的微孔膜材料。所得隔膜弹性形变量满足Δx/L>1.6%、厚度7μm、孔隙率37%、透气度值为135sec/100c。A diaphragm with high elastic deformation and a preparation method thereof, comprising mixing 82% paraffin oil with a mass proportion of 18% and polyethylene with an average molecular weight of 1.5 million, heating and melting to form a uniform mixture, and then cooling down Phase separation to obtain a membrane, and then heating the membrane to a temperature close to the melting point, and performing bidirectional simultaneous stretching (7 times MD stretching, 7 times TD stretching) with a stretching ratio of 49 for the first time to orient the molecular chains, Followed by heat preservation for a certain period of time, the residual liquid hydrocarbons were eluted with volatile solvent dichloromethane, then dried, and finally through the second transverse stretching (TD stretching ratio 1.4 times), the area retracted by 18% after setting, the whole process By controlling the speed difference between the front and rear rollers to be less than 0.3m/min, the maximum value of the tension in the longitudinal process is <400N/m, and the maximum value of the transverse tension of the diaphragm is controlled by the shearing roller or pressing roller to <100N/m, and the interpenetrating and high Microporous membrane material with elastic deformation. The elastic deformation of the obtained diaphragm satisfies Δx/L > 1.6%, a thickness of 7 μm, a porosity of 37%, and an air permeability of 135 sec/100c.
实施例3Example 3
本实施例与实施例2的区别在于,石蜡油占比80%,聚乙烯占比20%,第二次横向拉伸(TD拉伸倍率1.45倍),定型后面积回缩20%。所得隔膜弹性形变量满足Δx/L>1.3%、厚度12μm、孔隙率40%、透气度值为155sec/100c。The difference between this embodiment and embodiment 2 is that paraffin oil accounts for 80%, polyethylene accounts for 20%, and the second transverse stretching (TD stretching ratio is 1.45 times), the area shrinks back by 20% after setting. The elastic deformation of the obtained diaphragm satisfies Δx/L>1.3%, a thickness of 12 μm, a porosity of 40%, and an air permeability of 155 sec/100c.
此外,通过实施例1-3的工艺条件能够制备出3~20μm隔膜(基膜),隔膜弹性形变量满足Δx/L>0.8%、孔隙率25~70%、透气度值为50~400sec/100c。In addition, the 3-20 μm diaphragm (base film) can be prepared through the process conditions of Examples 1-3, the elastic deformation of the diaphragm satisfies Δx/L>0.8%, the porosity is 25-70%, and the air permeability value is 50-400sec/ 100c.
实施例4Example 4
一种高弹性形变量隔膜及其制备方法,涂层的成分和含量为:D50为0.6μm的氧化铝92份、改性聚丙烯酸4.5份、聚乙烯醇2.5份、聚丙烯酸铵1份,通过搅拌配制固含量为30%的水性涂覆浆料,将实施例1制备的9μm作为基膜,通过MCD型涂布机,将上述水性涂层的组合浆料经过凹版式涂布在基膜单侧,并最终经过烘箱烘烤后,涂层厚度为3μm,整个过程通过临近前后辊筒速度差控制小于0.2m/min,使得纵向过程张力最大值<100N/m,通过剪辊或压辊加持力控制横向张力最大值<50N/m,制备出相互贯通且高弹性形变量的微孔膜材料。所得隔膜弹性形变量满足Δx/L>0.5%,厚度12μm、透气度值为170sec/100c。A diaphragm with high elastic deformation and its preparation method. The composition and content of the coating are: 92 parts of alumina with a D50 of 0.6 μm, 4.5 parts of modified polyacrylic acid, 2.5 parts of polyvinyl alcohol, and 1 part of ammonium polyacrylate. Stir to prepare a water-based coating slurry with a solid content of 30%, use the 9 μm prepared in Example 1 as the base film, and use the MCD type coater to gravure-coat the combined slurry of the above-mentioned water-based coating on the base film sheet. side, and finally after being baked in an oven, the coating thickness is 3 μm. The speed difference between the front and rear rollers is controlled to be less than 0.2m/min during the whole process, so that the maximum tension in the longitudinal process is less than 100N/m. The maximum value of the transverse tension is controlled by force <50N/m, and the microporous membrane material with interpenetration and high elastic deformation is prepared. The elastic deformation of the obtained diaphragm satisfies Δx/L>0.5%, the thickness is 12 μm, and the air permeability is 170 sec/100c.
实施例5Example 5
一种高弹性形变量隔膜及其制备方法,取15重量份聚偏氟乙烯胶液(质量分数为20%)和20重量份聚酰亚胺胶液(质量分数为10%),溶解到57重量份二甲基乙酰胺和三丙二醇混合液中(其中,二甲基乙酰胺、三丙二 醇与水的重量比为15:70:30),之后依次加入20重量份硅烷偶联剂改性的D50为0.64μm氧化铝、3重量份乳液型丙烯酸酯类粘结剂(固含量为40%,25℃粘度为20cps~200cps),室温混合搅拌1h,得到白色粘稠涂覆浆料。将实施例2制备的7μm作为基膜,通过MCD型涂布机,采用凹版涂覆方式在基膜的一侧涂覆上述涂覆浆料,之后浸入到22℃的凝固液(二甲基乙酰胺、三丙二醇与水的重量比28:12:60),待聚烯烃多孔膜表面的湿膜先固化,依次水洗、干燥,得到复合隔膜,复合隔膜出水槽液面后至干燥过程,涂层厚度为2μm,整个过程通过临近前后辊筒速度差控制小于0.1m/min,使得纵向过程张力最大值<120N/m,通过剪辊或压辊加持力控制横向张力最大值<60N/m,制备出相互贯通且高弹性形变量的微孔膜材料。所得隔膜弹性形变量满足Δx/L>1.0%,厚度9μm、透气度值为180sec/100c。A high elastic deformation diaphragm and a preparation method thereof, 15 parts by weight of polyvinylidene fluoride glue solution (20% by mass fraction) and 20 parts by weight of polyimide glue solution (10% by mass fraction), are dissolved to 57 In the mixed liquid of dimethylacetamide and tripropylene glycol (wherein, the weight ratio of dimethylacetamide, tripropylene glycol and water is 15:70:30), add 20 parts by weight of silane coupling agent modified D50 is 0.64 μm alumina, 3 parts by weight of emulsion-type acrylate binder (solid content is 40%, viscosity is 20cps-200cps at 25°C), mixed and stirred at room temperature for 1 hour to obtain a white viscous coating slurry. The 7 μm prepared in Example 2 is used as the base film, and the above-mentioned coating slurry is coated on one side of the base film by means of gravure coating by an MCD type coater, and then immersed in a coagulation solution (dimethyl ethyl alcohol) at 22 ° C. The weight ratio of amide, tripropylene glycol and water is 28:12:60), and the wet film on the surface of the polyolefin porous membrane is first cured, washed with water and dried in turn to obtain a composite diaphragm. The thickness is 2μm, and the speed difference between the front and rear rollers is controlled to be less than 0.1m/min in the whole process, so that the maximum tension in the longitudinal process is <120N/m, and the maximum tension in the transverse direction is controlled by the shearing roller or pressing roller to <60N/m. A microporous membrane material with interpenetration and high elastic deformation. The elastic deformation of the obtained diaphragm satisfies Δx/L>1.0%, the thickness is 9 μm, and the air permeability is 180 sec/100c.
实施例6Example 6
一种高弹性形变量隔膜及其制备方法,向质量分数为1.5%、表观粘度为300cp的芳纶原液中分散0.1倍芳纶质量、D50为0.8μm的氧化铝粉,通过高速分散乳化机搅拌30min,在1000目滤网过滤后得到均匀的对位芳纶浆料。将实施例3制备的12μm作为基膜,通过MCD型涂布机,采用凹版涂覆方式在基膜的一侧涂覆上述对位芳纶浆料,制备的涂覆膜在60℃、60%RH的饱和蒸汽氛围下停留30s,随后进入纯水槽水洗120s,然后进入75℃的烘箱干燥60s,涂层厚度为4μm。整个过程通过临近前后辊筒速度差控制小于0.15m/min,使得纵向过程张力最大值<110N/m,通过剪辊或压辊加持力横向张力最大值<80N/m,制备出相互贯通且高弹性形变量的微孔膜材料。所得隔膜弹性形变量满足Δx/L>0.8%,厚度16μm、透气度值为260sec/100c。A diaphragm with high elastic deformation and its preparation method, dispersing alumina powder with 0.1 times the mass of aramid fiber and D50 of 0.8 μm in the aramid fiber stock solution with a mass fraction of 1.5% and an apparent viscosity of 300cp, and passing it through a high-speed dispersing emulsifier Stir for 30 minutes, and obtain a uniform para-aramid slurry after filtering through a 1000-mesh filter. The 12 μm prepared in Example 3 is used as the base film, and the above-mentioned para-aramid slurry is coated on one side of the base film by means of gravure coating through an MCD type coating machine. Stay in the saturated steam atmosphere of RH for 30s, then wash in a pure water tank for 120s, and then dry in an oven at 75°C for 60s, with a coating thickness of 4μm. In the whole process, the speed difference between the front and rear rollers is controlled to be less than 0.15m/min, so that the maximum tension in the longitudinal process is less than 110N/m, and the maximum tension in the transverse direction is less than 80N/m through the holding force of the shearing roller or pressing roller. Microporous membrane material with elastic deformation. The elastic deformation of the obtained diaphragm satisfies Δx/L>0.8%, the thickness is 16 μm, and the air permeability is 260 sec/100c.
最后应说明的是:以上各实施例仅用以说明本发明的技术方案,而非对其限制;尽管参照前述各实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行 修改,或者对其中部分或者全部技术特征进行等同替换;而这些修改或者替换,并不使相应技术方案的本质脱离本发明各实施例技术方案的范围。Finally, it should be noted that: the above embodiments are only used to illustrate the technical solutions of the present invention, rather than limiting them; although the present invention has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that: It is still possible to modify the technical solutions described in the foregoing embodiments, or perform equivalent replacements for some or all of the technical features; and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the technical solutions of the various embodiments of the present invention. scope.
Claims (10)
- 一种高弹性形变量隔膜,其特征在于,所述高弹性形变量隔膜包括:基膜,或,基膜与置于基膜至少一面上的涂层;A high elastic deformation diaphragm, characterized in that the high elastic deformation diaphragm comprises: a base film, or a base film and a coating placed on at least one side of the base film;所述高弹性形变量隔膜的弹性形变量满足:Δx/L>0.2%;The elastic deformation of the high elastic deformation diaphragm satisfies: Δx/L>0.2%;其中,L为原始长度,单位:米;Δx为弹性形变量,单位:米。Among them, L is the original length, unit: meter; Δx is the elastic deformation, unit: meter.
- 根据权利要求1所述的高弹性形变量隔膜,其特征在于,所述基膜的厚度为3~20μm;和/或,The high elastic deformation diaphragm according to claim 1, characterized in that, the thickness of the base film is 3-20 μm; and/or,所述涂层的厚度为0.1~6μm。The thickness of the coating is 0.1-6 μm.
- 一种权利要求1或2所述的高弹性形变量隔膜的制备方法,其特征在于,所述基膜采用湿法或干法工艺制备;A method for preparing the high elastic deformation diaphragm according to claim 1 or 2, wherein the base film is prepared by a wet or dry process;湿法工艺包括以下步骤:The wet process includes the following steps:将将液态烃与聚烯烃树脂混合按照配方比例预处理,或直接输送至挤出系统,加热熔融形成均匀的混合物;混合熔体挤出至流延辊降温,进行相分离,冷却成型,制得膜片;再将膜片加热至接近熔点温度,进行双向同步或者分步拉伸使分子链取向,保温、定型;溶剂洗脱残留的液态烃,洗脱后将膜移出溶剂,干燥,然后再横向拉伸、定型、回缩,制备出相互贯通的微孔膜;The liquid hydrocarbon and polyolefin resin are mixed according to the formula ratio and pretreated, or directly transported to the extrusion system, heated and melted to form a uniform mixture; the mixed melt is extruded to the casting roll to cool down, phase separated, cooled and formed, and obtained Diaphragm; then heat the membrane to a temperature close to the melting point, carry out two-way synchronous or step-by-step stretching to make the molecular chain orientation, heat preservation, and finalization; the solvent elutes the residual liquid hydrocarbons, and after elution, the membrane is removed from the solvent, dried, and then Transverse stretching, shaping, and retraction to prepare interpenetrating microporous membranes;其中,湿法制备过程需满足条件1和/或条件2:Among them, the wet preparation process needs to meet condition 1 and/or condition 2:条件1:混合浆料中聚烯烃的固含量<40%,聚烯烃的粘均分子量(万)/拉伸倍率>0.04,且聚烯烃的粘均分子量(万)/MD拉伸倍率>0.04;聚烯烃的粘均分子量(万)/TD拉伸倍率>1;Condition 1: The solid content of polyolefin in the mixed slurry is less than 40%, the viscosity-average molecular weight (10,000)/stretch ratio of polyolefin>0.04, and the viscosity-average molecular weight (10,000)/MD stretch ratio of polyolefin>0.04; The viscosity-average molecular weight of polyolefin (10,000)/TD draw ratio>1;条件2:回缩步骤控制回缩面积比例>1%;Condition 2: the shrinkage step controls the shrinkage area ratio > 1%;或,干法工艺包括以下步骤:Alternatively, the dry process includes the following steps:将聚烯烃树脂及添加剂原料按照配方比例预处理,或直接输送至挤出系统,原料在挤出系统中,经熔融塑化后从模头挤出熔体至流延辊降温, 冷却成型,形成特定结晶结构的片材,将片材进行热处理后得到硬弹性薄膜,随后进行冷拉伸和热拉伸后,回缩、定型形成基膜;The polyolefin resin and additive raw materials are pretreated according to the formula ratio, or directly transported to the extrusion system. In the extrusion system, the raw materials are melted and plasticized, and then the melt is extruded from the die to the casting roll to cool down, cooled and formed, and formed For sheets with a specific crystalline structure, the sheet is heat-treated to obtain a hard elastic film, followed by cold stretching and hot stretching, retracting and shaping to form a base film;其中,干法制备过程需满足条件1’和/或条件2’:Among them, the dry preparation process needs to meet condition 1' and/or condition 2':条件1’:聚烯烃的粘均分子量(万)/拉伸倍率>0.04;Condition 1': viscosity-average molecular weight (10,000)/stretch ratio of polyolefin > 0.04;条件2’:回缩步骤控制回缩面积比例>1%。Condition 2': the shrinkage step controls the shrinkage area ratio > 1%.
- 根据权利要求3所述的制备方法,其特征在于,湿法制备过程还需要满足条件3:The preparation method according to claim 3, wherein the wet preparation process also needs to meet condition 3:条件3:除去挤出、拉伸段的工艺,其它过程控制纵向张力<500N/m,横向张力<100N/m。Condition 3: Excluding the process of extrusion and stretching, other processes control the longitudinal tension <500N/m, and the transverse tension <100N/m.
- 根据权利要求3所述的制备方法,其特征在于,干法制备过程还需要满足条件3’:preparation method according to claim 3, is characterized in that, dry preparation process also needs to satisfy condition 3':条件3’:除去挤出、拉伸段的工艺,其它过程控制纵向张力<1000N/m,横向张力<100N/m。Condition 3': remove the process of extrusion and stretching, and control the longitudinal tension <1000N/m and transverse tension <100N/m in other processes.
- 根据权利要求3所述的制备方法,其特征在于,所述制备方法还包括:在基膜单侧或两侧增加涂层的步骤:涂覆浆料涂覆在基膜表面,经过干燥或处理后干燥形成,涂覆浆料由无机陶瓷颗粒、有机聚合物材料中的一种或混合组成;The preparation method according to claim 3, characterized in that, the preparation method further comprises: the step of adding a coating on one side or both sides of the base film: the coating slurry is coated on the surface of the base film, dried or treated Formed after drying, the coating slurry is composed of one or a mixture of inorganic ceramic particles, organic polymer materials;其中,增加涂层的步骤需要满足条件4:Among them, the step of adding coating needs to meet condition 4:当无机陶瓷颗粒的重量占比>80%时,要求无机陶瓷颗粒0.1μm≤D50≤2.0μm;When the weight ratio of inorganic ceramic particles is >80%, the inorganic ceramic particles are required to be 0.1μm≤D50≤2.0μm;当无机陶瓷颗粒的重量占比在30%-80%时,要求无机陶瓷颗粒0.01μm≤D50≤4μm;When the weight ratio of inorganic ceramic particles is 30%-80%, the inorganic ceramic particles are required to be 0.01μm≤D50≤4μm;当无机陶瓷颗粒的重量占比<30%时,要求无机陶瓷颗粒D50≤10μm。When the weight ratio of the inorganic ceramic particles is less than 30%, the D50 of the inorganic ceramic particles is required to be less than or equal to 10 μm.
- 根据权利要求6所述的制备方法,其特征在于,增加涂层的步骤还需要满足条件5:在涂覆、干燥过程或在涂覆、处理、干燥过程控制纵向张力<150N/m,横向张力<100N/m。The preparation method according to claim 6, characterized in that the step of adding the coating also needs to meet condition 5: during the coating and drying process or during the coating, treatment and drying process, the longitudinal tension is controlled <150N/m, and the transverse tension is less than 150N/m. <100N/m.
- 根据权利要求6所述的制备方法,其特征在于,无机陶瓷颗粒包括氧化铝、勃姆石、碳酸钙、水滑石、蒙脱土、尖晶石、莫来石、二氧化钛、二氧化硅、二氧化锆、氧化镁、氧化钙、氧化铍、氢氧化镁、氮化硼、氮化硅、氮化铝、氮化钛、碳化硼、碳化硅、碳化锆中的一种或几种。The preparation method according to claim 6, wherein the inorganic ceramic particles include alumina, boehmite, calcium carbonate, hydrotalcite, montmorillonite, spinel, mullite, titanium dioxide, silicon dioxide, One or more of zirconia, magnesium oxide, calcium oxide, beryllium oxide, magnesium hydroxide, boron nitride, silicon nitride, aluminum nitride, titanium nitride, boron carbide, silicon carbide, and zirconium carbide.
- 根据权利要求6所述的制备方法,其特征在于,有机聚合物材料包括聚酰亚胺、聚醚酰亚胺、芳纶、芳砜纶、聚偏二氟乙烯、聚甲基丙烯酸甲酯、聚环氧乙烷、聚丙烯腈、聚偏氟乙烯、聚偏氟乙烯-六氟丙烯有机粉料或悬浮液中的一种或几种。The preparation method according to claim 6, wherein the organic polymer material comprises polyimide, polyetherimide, aramid fiber, polysulfone fiber, polyvinylidene fluoride, polymethyl methacrylate, One or more of polyethylene oxide, polyacrylonitrile, polyvinylidene fluoride, polyvinylidene fluoride-hexafluoropropylene organic powder or suspension.
- 一种锂离子电池,其特征在于,所述锂离子电池包括权利要求1或2所述的高弹性形变量隔膜或权利要求3-9任一项所述的制备方法制备得到的高弹性形变量隔膜。A lithium-ion battery, characterized in that, the lithium-ion battery comprises the high elastic deformation diaphragm described in claim 1 or 2 or the high elastic deformation prepared by the preparation method described in any one of claims 3-9 diaphragm.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202111589284.9A CN114243221B (en) | 2021-12-23 | 2021-12-23 | High-elasticity deformation diaphragm and preparation method thereof |
CN202111589284.9 | 2021-12-23 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2023115625A1 true WO2023115625A1 (en) | 2023-06-29 |
Family
ID=80761992
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/CN2021/142772 WO2023115625A1 (en) | 2021-12-23 | 2021-12-30 | Separator having large elastic deformation quantity and preparation method therefor |
Country Status (2)
Country | Link |
---|---|
CN (1) | CN114243221B (en) |
WO (1) | WO2023115625A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN118054159A (en) * | 2024-04-15 | 2024-05-17 | 深圳欣界能源科技有限公司 | Composite elastic diaphragm and preparation method and application thereof |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115995656B (en) * | 2023-03-23 | 2023-05-26 | 泰州衡川新能源材料科技有限公司 | Preparation method and coating device of lithium ion battery diaphragm |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013187326A1 (en) * | 2012-06-13 | 2013-12-19 | 東レ株式会社 | Porous polypropylene film, separator for electricity storage devices, and electricity storage device |
CN103762327A (en) * | 2014-01-17 | 2014-04-30 | 苏州鼎机新能源材料科技有限公司 | Lithium ion battery separator and production technology thereof |
CN106415885A (en) * | 2014-06-11 | 2017-02-15 | 东丽电池隔膜株式会社 | Battery separator and production method therefor |
CN111391267A (en) * | 2020-03-25 | 2020-07-10 | 石狮申泰新材料科技有限公司 | Dry-process single-drawing production process of lithium battery diaphragm |
Family Cites Families (23)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS596469B2 (en) * | 1979-02-05 | 1984-02-10 | 日本原子力研究所 | Manufacturing method for battery diaphragm with excellent dimensional stability |
CN102683628B (en) * | 2011-03-09 | 2016-02-03 | 天津东皋膜技术有限公司 | Coextru-lamination barrier film containing nanometer precrosslinked rubber micro mist and use its lithium ion battery |
CN102751459B (en) * | 2011-04-22 | 2016-03-23 | 天津东皋膜技术有限公司 | Rear cross-linked rubber, the micro-porous septum of composite polyolefine material nanometer and manufacture method thereof |
US20140057057A1 (en) * | 2011-12-02 | 2014-02-27 | Mitsubishi Plastics, Inc., | Process for producing a laminated porous film |
CN102709584B (en) * | 2012-06-20 | 2014-11-26 | 东莞市雅康精密机械有限公司 | Battery coiler |
CN103199300B (en) * | 2013-04-22 | 2015-06-10 | 上海双奥能源技术有限公司 | Coated lithium ion battery diaphragm |
CN103633269A (en) * | 2013-08-22 | 2014-03-12 | 东莞市易威科电子科技有限公司 | Yellow ceramic diaphragm for lithium ion battery and application thereof |
CN103633272B (en) * | 2013-12-10 | 2016-01-06 | 深圳市星源材质科技股份有限公司 | A kind of preparation method of micro-pore septum and micro-pore septum |
JP2017088837A (en) * | 2015-11-11 | 2017-05-25 | 有限会社ケー・イー・イー | Low heat shrinkable polyolefin microporous film and manufacturing method therefor |
CN105602309B (en) * | 2015-12-28 | 2018-05-08 | 深圳市星源材质科技股份有限公司 | A kind of sub- coating paste of high resiliency diversion and its lithium ion battery separator preparation method |
TWI770004B (en) * | 2016-03-29 | 2022-07-11 | 日商東麗股份有限公司 | Polyolefin microporous membrane and method for producing the same, separator for battery and method for producing the same |
CN106680469A (en) * | 2016-12-27 | 2017-05-17 | 北方华锦化学工业集团有限公司 | Evaluation method of special polypropylene resin for lithium battery diaphragm |
CN106654125A (en) * | 2017-01-24 | 2017-05-10 | 厦门大学 | Method for preparing modified ceramic diaphragm through dopamine compound adhesive and application thereof |
CN106981608B (en) * | 2017-05-08 | 2021-06-11 | 深圳市星源材质科技股份有限公司 | Preparation method of multilayer microporous membrane for lithium ion battery |
CN108389999A (en) * | 2018-01-23 | 2018-08-10 | 惠州市旭然新能源有限公司 | Organic and inorganic composite coated porous separation film, preparation method and its lithium ion battery |
CN109103397A (en) * | 2018-09-28 | 2018-12-28 | 河南福森新能源科技有限公司 | A kind of preparation method of lithium ion battery ceramic coating membrane |
CN109461597B (en) * | 2018-11-13 | 2020-09-11 | 东莞东阳光科研发有限公司 | Flexible supercapacitor and preparation method of electrode and diaphragm thereof |
CN110911617A (en) * | 2019-12-10 | 2020-03-24 | 安徽新衡新材料科技有限公司 | High-toughness polyolefin lithium ion battery diaphragm and preparation method thereof |
CN112531292B (en) * | 2020-12-11 | 2023-03-31 | 宁波启新精合新能源研究院有限公司 | Lithium ion battery diaphragm prepared from inorganic-organic composite material |
CN112993490B (en) * | 2021-03-03 | 2023-06-09 | 广州鹏辉能源科技股份有限公司 | Lithium battery diaphragm and preparation method and application thereof |
CN113067101B (en) * | 2021-03-19 | 2022-07-05 | 江苏厚生新能源科技有限公司 | High-rigidity lithium ion battery diaphragm and preparation method thereof |
CN112864528B (en) * | 2021-04-26 | 2021-07-13 | 江苏厚生新能源科技有限公司 | Biaxial tension coating microporous diaphragm for lithium ion battery and preparation method thereof |
CN113594629B (en) * | 2021-07-13 | 2024-06-07 | 苏州捷力新能源材料有限公司 | High-temperature-resistant coating film, preparation method and electrochemical device thereof |
-
2021
- 2021-12-23 CN CN202111589284.9A patent/CN114243221B/en active Active
- 2021-12-30 WO PCT/CN2021/142772 patent/WO2023115625A1/en unknown
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013187326A1 (en) * | 2012-06-13 | 2013-12-19 | 東レ株式会社 | Porous polypropylene film, separator for electricity storage devices, and electricity storage device |
CN103762327A (en) * | 2014-01-17 | 2014-04-30 | 苏州鼎机新能源材料科技有限公司 | Lithium ion battery separator and production technology thereof |
CN106415885A (en) * | 2014-06-11 | 2017-02-15 | 东丽电池隔膜株式会社 | Battery separator and production method therefor |
CN111391267A (en) * | 2020-03-25 | 2020-07-10 | 石狮申泰新材料科技有限公司 | Dry-process single-drawing production process of lithium battery diaphragm |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN118054159A (en) * | 2024-04-15 | 2024-05-17 | 深圳欣界能源科技有限公司 | Composite elastic diaphragm and preparation method and application thereof |
Also Published As
Publication number | Publication date |
---|---|
CN114243221A (en) | 2022-03-25 |
CN114243221B (en) | 2022-10-11 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US11603443B2 (en) | Composite porous membrane and preparation method therefor and use thereof | |
WO2023115625A1 (en) | Separator having large elastic deformation quantity and preparation method therefor | |
CN110350155B (en) | Composite microporous membrane comprising nanofibrous porous layer oriented in transverse stretching direction | |
CN112531285A (en) | High-temperature-resistant para-aramid coated lithium ion battery diaphragm and preparation method thereof | |
CN109509856B (en) | Aromatic polyamide microporous membrane and preparation method and application thereof | |
WO2013091297A1 (en) | Microporous membrane of polyethylene-based composite material with adhesion under hot pressing | |
CN110343278B (en) | Composite polypropylene microporous membrane, preparation method thereof and lithium ion battery diaphragm comprising composite polypropylene microporous membrane | |
KR102327715B1 (en) | Polyolefin porous membrane and its manufacturing method | |
CN107808943B (en) | Multilayer polyolefin microporous diaphragm and preparation method thereof | |
WO2023159836A1 (en) | High-breakdown-strength aramid fiber separator, preparation method therefor and use thereof | |
WO2012061963A1 (en) | Porous membrane and preparation method thereof | |
KR102584617B1 (en) | Lithium ion battery separator, method of manufacturing same, and lithium ion battery manufactured thereby | |
WO2013097311A1 (en) | Microporous membrane of polyvinyl composite material having hot pressing adhesion | |
CN111086181A (en) | Preparation method of lithium battery diaphragm | |
WO2013078890A1 (en) | Method for preparing power lithium battery diaphragm | |
TW201815921A (en) | Microporous membrane, lithium ion secondary battery, and microporous membrane production method | |
CN110943194B (en) | Preparation method and coating application of lithium battery diaphragm with controllable surface structure | |
CN114142160B (en) | Nano ceramic-polypropylene composite battery diaphragm and preparation method thereof | |
WO2023115624A1 (en) | Separator having high section structure consistency and preparation method therefor | |
JP2019102400A (en) | Multilayer separator, and its wound body and manufacturing method | |
CN115312973B (en) | Polyolefin porous membrane and preparation method thereof, battery diaphragm and electrochemical device | |
JP2022517293A (en) | Method for Producing Polyolefin Porous Membrane | |
WO2023011293A1 (en) | Composite separator, electrochemical apparatus, electronic device, and mobile terminal | |
CN115764159A (en) | Three-layer lithium battery diaphragm and preparation method thereof | |
CN112864531B (en) | Diaphragm, preparation method of diaphragm and battery |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 21968750 Country of ref document: EP Kind code of ref document: A1 |
|
NENP | Non-entry into the national phase |
Ref country code: DE |