TWI488742B - Laminated porous film, preparation method thereof and separator for secondary cell comprising same - Google Patents
Laminated porous film, preparation method thereof and separator for secondary cell comprising same Download PDFInfo
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- TWI488742B TWI488742B TW102114802A TW102114802A TWI488742B TW I488742 B TWI488742 B TW I488742B TW 102114802 A TW102114802 A TW 102114802A TW 102114802 A TW102114802 A TW 102114802A TW I488742 B TWI488742 B TW I488742B
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- wax
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- 238000002360 preparation method Methods 0.000 title 1
- 229920005989 resin Polymers 0.000 claims description 55
- 239000011347 resin Substances 0.000 claims description 55
- 239000001993 wax Substances 0.000 claims description 41
- -1 polypropylene Polymers 0.000 claims description 28
- 238000002844 melting Methods 0.000 claims description 26
- 230000008018 melting Effects 0.000 claims description 26
- 239000004743 Polypropylene Substances 0.000 claims description 24
- 229920001155 polypropylene Polymers 0.000 claims description 24
- 239000003484 crystal nucleating agent Substances 0.000 claims description 21
- 229920013716 polyethylene resin Polymers 0.000 claims description 19
- 239000004200 microcrystalline wax Substances 0.000 claims description 14
- 235000019808 microcrystalline wax Nutrition 0.000 claims description 14
- 239000004698 Polyethylene Substances 0.000 claims description 13
- 229920000573 polyethylene Polymers 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 11
- 230000035699 permeability Effects 0.000 claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 10
- 239000000155 melt Substances 0.000 claims description 10
- 238000004898 kneading Methods 0.000 claims description 7
- 239000012188 paraffin wax Substances 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 6
- MBSRTKPGZKQXQR-UHFFFAOYSA-N 2-n,6-n-dicyclohexylnaphthalene-2,6-dicarboxamide Chemical compound C=1C=C2C=C(C(=O)NC3CCCCC3)C=CC2=CC=1C(=O)NC1CCCCC1 MBSRTKPGZKQXQR-UHFFFAOYSA-N 0.000 claims description 4
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- FMZUHGYZWYNSOA-VVBFYGJXSA-N (1r)-1-[(4r,4ar,8as)-2,6-diphenyl-4,4a,8,8a-tetrahydro-[1,3]dioxino[5,4-d][1,3]dioxin-4-yl]ethane-1,2-diol Chemical compound C([C@@H]1OC(O[C@@H]([C@@H]1O1)[C@H](O)CO)C=2C=CC=CC=2)OC1C1=CC=CC=C1 FMZUHGYZWYNSOA-VVBFYGJXSA-N 0.000 claims description 2
- 239000005995 Aluminium silicate Substances 0.000 claims description 2
- 239000005997 Calcium carbide Substances 0.000 claims description 2
- 150000007933 aliphatic carboxylic acids Chemical class 0.000 claims description 2
- 125000001931 aliphatic group Chemical group 0.000 claims description 2
- 235000012211 aluminium silicate Nutrition 0.000 claims description 2
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 claims description 2
- 239000004359 castor oil Substances 0.000 claims description 2
- 235000019438 castor oil Nutrition 0.000 claims description 2
- 229910000420 cerium oxide Inorganic materials 0.000 claims description 2
- 229940087101 dibenzylidene sorbitol Drugs 0.000 claims description 2
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 2
- 239000000194 fatty acid Substances 0.000 claims description 2
- 229930195729 fatty acid Natural products 0.000 claims description 2
- 235000011187 glycerol Nutrition 0.000 claims description 2
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 claims description 2
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims description 2
- SFJUBBVCCFTYMD-UHFFFAOYSA-N n-(5-benzamidonaphthalen-1-yl)benzamide Chemical compound C=1C=CC=CC=1C(=O)NC(C1=CC=C2)=CC=CC1=C2NC(=O)C1=CC=CC=C1 SFJUBBVCCFTYMD-UHFFFAOYSA-N 0.000 claims description 2
- MHPSPWKMGFPVKI-UHFFFAOYSA-N n-[4-(cyclohexanecarbonylamino)cyclohexyl]cyclohexanecarboxamide Chemical compound C1CCCCC1C(=O)NC(CC1)CCC1NC(=O)C1CCCCC1 MHPSPWKMGFPVKI-UHFFFAOYSA-N 0.000 claims description 2
- UXMBRQOBONMJIC-UHFFFAOYSA-N n-[4-(cyclohexanecarbonylamino)phenyl]cyclohexanecarboxamide Chemical compound C1CCCCC1C(=O)NC(C=C1)=CC=C1NC(=O)C1CCCCC1 UXMBRQOBONMJIC-UHFFFAOYSA-N 0.000 claims description 2
- BMMGVYCKOGBVEV-UHFFFAOYSA-N oxo(oxoceriooxy)cerium Chemical compound [Ce]=O.O=[Ce]=O BMMGVYCKOGBVEV-UHFFFAOYSA-N 0.000 claims description 2
- 239000000454 talc Substances 0.000 claims description 2
- 229910052623 talc Inorganic materials 0.000 claims description 2
- CLZWAWBPWVRRGI-UHFFFAOYSA-N tert-butyl 2-[2-[2-[2-[bis[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]amino]-5-bromophenoxy]ethoxy]-4-methyl-n-[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]anilino]acetate Chemical compound CC1=CC=C(N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)C(OCCOC=2C(=CC=C(Br)C=2)N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)=C1 CLZWAWBPWVRRGI-UHFFFAOYSA-N 0.000 claims description 2
- MHZGKXUYDGKKIU-UHFFFAOYSA-N Decylamine Chemical compound CCCCCCCCCCN MHZGKXUYDGKKIU-UHFFFAOYSA-N 0.000 claims 1
- 238000010030 laminating Methods 0.000 claims 1
- 239000012170 montan wax Substances 0.000 claims 1
- 239000010410 layer Substances 0.000 description 26
- 239000011342 resin composition Substances 0.000 description 7
- 239000013078 crystal Substances 0.000 description 6
- 235000019809 paraffin wax Nutrition 0.000 description 5
- 235000019271 petrolatum Nutrition 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 239000002356 single layer Substances 0.000 description 4
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000005266 casting Methods 0.000 description 3
- 229920001903 high density polyethylene Polymers 0.000 description 3
- 239000004700 high-density polyethylene Substances 0.000 description 3
- 229910052744 lithium Inorganic materials 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- VZXTWGWHSMCWGA-UHFFFAOYSA-N 1,3,5-triazine-2,4-diamine Chemical class NC1=NC=NC(N)=N1 VZXTWGWHSMCWGA-UHFFFAOYSA-N 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 239000013032 Hydrocarbon resin Substances 0.000 description 1
- 238000004566 IR spectroscopy Methods 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 125000002723 alicyclic group Chemical group 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 1
- OGBUMNBNEWYMNJ-UHFFFAOYSA-N batilol Chemical class CCCCCCCCCCCCCCCCCCOCC(O)CO OGBUMNBNEWYMNJ-UHFFFAOYSA-N 0.000 description 1
- 238000007707 calorimetry Methods 0.000 description 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 239000002178 crystalline material Substances 0.000 description 1
- 238000001739 density measurement Methods 0.000 description 1
- 238000000113 differential scanning calorimetry Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 229920001038 ethylene copolymer Polymers 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 229920006270 hydrocarbon resin Polymers 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000010954 inorganic particle Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000003077 lignite Substances 0.000 description 1
- 229920000092 linear low density polyethylene Polymers 0.000 description 1
- 239000004707 linear low-density polyethylene Substances 0.000 description 1
- 229920005679 linear ultra low density polyethylene Polymers 0.000 description 1
- 229920001684 low density polyethylene Polymers 0.000 description 1
- 239000004702 low-density polyethylene Substances 0.000 description 1
- 229920001179 medium density polyethylene Polymers 0.000 description 1
- 239000004701 medium-density polyethylene Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005504 petroleum refining Methods 0.000 description 1
- 229920005672 polyolefin resin Polymers 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
Classifications
-
- 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
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
- H01M10/4235—Safety or regulating additives or arrangements in electrodes, separators or electrolyte
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/32—Layered products comprising a layer of synthetic resin comprising 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
- H01M50/489—Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
-
- 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
- H01M50/449—Separators, membranes or diaphragms characterised by the material having a layered structure
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
- C08J2323/10—Homopolymers or copolymers of propene
- C08J2323/12—Polypropene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2423/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2423/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
- C08J2423/04—Homopolymers or copolymers of ethene
- C08J2423/06—Polyethene
-
- 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
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Cell Separators (AREA)
- Laminated Bodies (AREA)
Description
本發明係有關於一具有優異斷開(SD)及崩潰(BD)性質、以及高透氣性的積層多孔膜、一用於製造該積層多孔膜的方法、及一用於含該多孔膜之二次電池的隔離件。The present invention relates to a laminated porous film having excellent breaking (SD) and collapse (BD) properties, and high gas permeability, a method for producing the laminated porous film, and a method for containing the porous film. The separator of the secondary battery.
用於電池(電池組)之隔離件廣泛分類成聚丙烯(PP)單層隔離件、聚乙烯(PE)單層隔離件及PE/PP積層隔離件。就PP單層隔離件而言,斷開性質比較劣,但是崩潰性質良好。反之,就PE單層隔離件而言,係具有良好的斷開性質及劣崩潰性質。The separators for batteries (batteries) are widely classified into polypropylene (PP) single-layer separators, polyethylene (PE) single-layer separators, and PE/PP laminated separators. In the case of a PP single-layer separator, the breaking property is inferior, but the collapse property is good. On the contrary, in the case of PE single-layer separators, it has good breaking properties and poor collapse properties.
另一方面,由於具有一PE/PP積層結構的隔離件兼具PP之崩潰性能及PE之斷開性能,所以近年來,其等業經主要用以增補上述兩種產物的缺點。日本專利公開案第2010-61973號、第2010-61974號及第2010-120217號揭示一 使用β-晶體成核劑之主要由一PP樹脂、及一PE樹脂所組成的積層多孔膜,且含至少一選自以下所組成的群組:經改質的聚烯烴樹脂、脂環族飽和烴樹脂或其等之經改質產物、乙烯共聚物及蠟。On the other hand, since the separator having a PE/PP laminate structure has both the collapse property of PP and the disconnection property of PE, in recent years, it has been mainly used to supplement the disadvantages of the above two products. Japanese Patent Publication No. 2010-61973, No. 2010-61974 and No. 2010-120217 disclose one The β-crystal nucleating agent is a laminated porous film mainly composed of a PP resin and a PE resin, and contains at least one group selected from the group consisting of modified polyolefin resin, alicyclic saturated A modified product of a hydrocarbon resin or the like, an ethylene copolymer, and a wax.
然而,根據添加至該PE樹脂層的熱塑性樹膠,這些習知薄膜具有不同性質,因此當這些習知薄膜係以和習知方法相同的方式施用時,並不能充份地確保用於隔離件所需的透氣性,且會對該等製法造成限制。However, these conventional films have different properties depending on the thermoplastic gum added to the PE resin layer, and therefore, when these conventional films are applied in the same manner as the conventional methods, they are not sufficiently ensured for the separator. The breathability required, and will limit the method.
因此,本發明之一目標為提供一具有優異斷開及崩潰性質、以及高透氣性的積層多孔膜、一用於製造該積層多孔膜的方法、及一用於含該多孔膜之二次電池的隔離件。Accordingly, it is an object of the present invention to provide a laminated porous film having excellent breaking and collapse properties and high gas permeability, a method for producing the laminated porous film, and a secondary battery for containing the porous film. Isolation piece.
根據本發明之一方面,係提供一具有含以下2或多層之積層結構的積層多孔膜:1)含一聚丙烯樹脂及一β-晶體成核劑的第一樹脂層;及2)含一聚乙烯樹脂及具有90℃或更高之熔點及80%或更高之結晶度的蠟。According to an aspect of the invention, there is provided a laminated porous film having a laminate structure comprising 2 or more layers: 1) a first resin layer containing a polypropylene resin and a β-crystal nucleating agent; and 2) A polyethylene resin and a wax having a melting point of 90 ° C or higher and a crystallinity of 80% or more.
根據本發明之另一方面,係提供一用於製造該積層多孔膜之方法,其包含以下步驟:a)添加一聚丙烯樹脂及一β-晶體成核劑,並使其等經熔態揑揉,藉此製成第一樹脂;b)添加一聚乙烯樹脂及具有90℃或更高的熔點及80%或更高之結晶度之蠟,並使其等經揑揉,因此製成第二樹脂;c)分別擠製該第一樹脂及第二樹脂,且使其等進行積層化,藉此形成一含經積層之第一樹脂層及第二樹脂層的 非拉製薄片;及d)拉製該非拉製薄片。According to another aspect of the present invention, there is provided a method for producing the laminated porous film comprising the steps of: a) adding a polypropylene resin and a β-crystal nucleating agent, and subjecting them to a melt state.揉, thereby forming a first resin; b) adding a polyethylene resin and a wax having a melting point of 90 ° C or higher and a crystallinity of 80% or higher, and kneading the same, thereby making the first a second resin; c) separately extruding the first resin and the second resin, and stratifying the same, thereby forming a laminated first resin layer and a second resin layer a non-drawn sheet; and d) the non-drawn sheet is drawn.
根據本發明之另一方面,係提供一用於含該積層多孔膜之二次電池的隔離件。According to another aspect of the present invention, there is provided a separator for a secondary battery comprising the laminated porous film.
根據本發明該積層多孔膜可具有優異斷開及崩潰性質、以及高透氣性,且因此,可有效率地施用至一用於鋰二次電池等之隔離件。According to the present invention, the laminated porous film can have excellent breaking and collapse properties, and high gas permeability, and therefore, can be efficiently applied to a separator for a lithium secondary battery or the like.
下文,係描述一根據本發明之積層多孔膜。Hereinafter, a laminated porous film according to the present invention will be described.
根據本發明該積層多孔膜具有一含以下2或多層的積層結構:1)由一含一β-晶體成核劑之聚丙烯樹脂所製成的第一樹脂層;及2)由一含具有90℃或更高之熔點及80%或更高之結晶度的蠟之聚乙烯樹脂所製成的第二樹脂層。According to the present invention, the laminated porous film has a laminate structure comprising 2 or more layers: 1) a first resin layer made of a polypropylene resin containing a β-crystal nucleating agent; and 2) A second resin layer made of a polyethylene resin of a wax having a melting point of 90 ° C or higher and a crystallinity of 80% or more.
在本發明內,包含在該第一樹脂層內之該β-晶體成核劑可選自以下所組成的群組:N,N’-二環己基-2,6-萘二羧醯胺、N,N’-二環己基對苯二甲醯胺、N,N’-二環己烷羰基-對-苯二胺、N,N’-二苯甲醯基-1,5-二胺基萘、N,N’-二環己烷羰基-1,4-二胺基環己烷、N-環己基-4-苯甲醯胺及其等之混合物。較佳有用的β-晶體成核劑為N,N’-二環己基-2,6-萘二羧醯胺。In the present invention, the β-crystal nucleating agent contained in the first resin layer may be selected from the group consisting of N, N'-dicyclohexyl-2,6-naphthalenedicarbamide, N,N'-dicyclohexyl-p-xylamine, N,N'-dicyclohexanecarbonyl-p-phenylenediamine, N,N'-dibenzoyl-1,5-diamino Naphthalene, N,N'-dicyclohexanecarbonyl-1,4-diaminocyclohexane, N-cyclohexyl-4-benzamide, and mixtures thereof. A preferred useful β-crystal nucleating agent is N,N'-dicyclohexyl-2,6-naphthalenedicarbamide.
以100重量份該聚丙烯樹脂計,該β-晶體成核劑 的添加量較佳自0.0001至5重量份,且更佳0.001至1重量份。The β-crystal nucleating agent is based on 100 parts by weight of the polypropylene resin The amount added is preferably from 0.0001 to 5 parts by weight, and more preferably from 0.001 to 1 part by weight.
用於本發明之該聚丙烯樹脂較佳具有一自1至20克/10分鐘的熔化指數。The polypropylene resin used in the present invention preferably has a melt index of from 1 to 20 g/10 minutes.
在本發明內,可藉添加蠟至該聚乙烯樹脂而提供呈多孔結構形式之該第二樹脂層,該蠟具有90℃或更高,且較佳95℃或更高的熔點,且,例如該蠟之熔點可在自90至150℃之範圍內。而且,該蠟具有80%或更高,且較佳85%或更高的結晶度,因此使其可具有適於一用於鋰二次電池之隔離件的透氣性。In the present invention, the second resin layer in a porous structure may be provided by adding a wax to the polyethylene resin, the wax having a melting point of 90 ° C or higher, and preferably 95 ° C or higher, and, for example, The wax may have a melting point in the range of from 90 to 150 °C. Moreover, the wax has a crystallinity of 80% or more, and preferably 85% or more, so that it can have a gas permeability suitable for a separator for a lithium secondary battery.
若該蠟的熔點小於90℃,則在一拉製法期間以縱向(MD)熔化該蠟,因此會阻礙鄰近該蠟之聚丙烯樹脂表面的多孔結構之形成,所以不能確保該積層多孔膜得到充份的透氣性。在本情況下,為了確保充份的透氣性,雖然該MD拉製溫度應該被設定於小於90℃,但是於小於90℃之溫度下,該薄膜的崩潰性能會增加,其會非所欲地使生產率及膜形成安定性變質。因此,用於本發明之該蠟的熔點應該是90℃或更高。If the melting point of the wax is less than 90 ° C, the wax is melted in the machine direction (MD) during the drawing process, thereby hindering the formation of the porous structure on the surface of the polypropylene resin adjacent to the wax, so that the laminated porous film cannot be ensured to be charged. Part of the breathability. In this case, in order to ensure sufficient gas permeability, although the MD drawing temperature should be set to less than 90 ° C, at a temperature of less than 90 ° C, the collapse performance of the film may increase, which may be undesired. The productivity and film formation stability are deteriorated. Therefore, the melting point of the wax used in the present invention should be 90 ° C or higher.
而且,若該蠟的結晶度小於80%,則在該拉製法內,此蠟係連同該聚乙烯層經拉製,使其不可能形成該聚乙烯層的合適多孔結構,且因此不能得到充份的透氣性。所以,用於本發明之該蠟的結晶度應該是80%或更高。可使用IR光譜學、X射線繞射、密度測定法、量熱法等測定該結晶度。例如可使用差示掃描式量熱法(DSC),且明確地說,可測定一試樣的熔化焓(△H f ),然後與一完全結晶狀材 料之熔化焓(△H f )比較以計算該試樣之結晶度。Moreover, if the crystallinity of the wax is less than 80%, in the drawing method, the wax system is drawn together with the polyethylene layer, making it impossible to form a suitable porous structure of the polyethylene layer, and thus cannot be charged. Part of the breathability. Therefore, the crystallinity of the wax used in the present invention should be 80% or more. The crystallinity can be measured using IR spectroscopy, X-ray diffraction, density measurement, calorimetry, or the like. For example, differential scanning calorimetry (DSC) can be used, and specifically, the melting enthalpy (ΔH f ) of a sample can be determined and then compared with the melting enthalpy (ΔH f ) of a completely crystalline material. The crystallinity of the sample was calculated.
該具有在上述範圍內之熔點及結晶度的蠟可以是極性蠟或非極性蠟,且其等之特定實例可包括聚丙烯蠟、聚乙烯蠟、蓖麻油蠟、微晶狀蠟、石蠟、褐煤蠟、純地蠟、經取代之醯胺蠟、或其等之混合物。特別有用的蠟為微晶狀蠟。該微晶狀蠟為藉在石油精煉方法中進行石蠟酯的去油而製成的蠟類型。與主要含直鏈烷烴之廣泛已知的石蠟比較,微晶狀蠟含有較高比率之以異烷烴為主之分支鏈烴及環烷烴。不像具有大晶體之石蠟,該微晶狀蠟具有微細晶體,且係含具有高分子量的飽和脂肪族烴。與石蠟比較,該微晶狀蠟顯示較暗的色彩,且具有較高黏度、密度、黏著性、及彈性以及較高分子量及熔點。該微晶狀蠟之彈性與黏著性係與其所含的非直鏈組份有關。由於該微晶狀蠟的晶體結構小且細緻,因此比石蠟更具可撓性。The wax having a melting point and crystallinity within the above range may be a polar wax or a non-polar wax, and specific examples thereof may include polypropylene wax, polyethylene wax, castor oil wax, microcrystalline wax, paraffin wax, lignite. A wax, a purely wax, a substituted guanamine wax, or a mixture thereof. Particularly useful waxes are microcrystalline waxes. The microcrystalline wax is a type of wax produced by deoiling a paraffin ester in a petroleum refining process. The microcrystalline wax contains a higher proportion of isoparaffin-dominated branched chain hydrocarbons and naphthenes than the widely known paraffin wax which mainly contains linear paraffins. Unlike paraffin waxes having large crystals, the microcrystalline wax has fine crystals and contains saturated aliphatic hydrocarbons having a high molecular weight. Compared to paraffin wax, the microcrystalline wax exhibits a darker color with higher viscosity, density, adhesion, and elasticity as well as higher molecular weight and melting point. The elasticity and adhesion of the microcrystalline wax are related to the non-linear components contained therein. Since the crystallinity of the microcrystalline wax is small and fine, it is more flexible than paraffin wax.
以該第二樹脂層的重量計,此蠟的添加量較佳為自5至30重量%,且更佳5至20重量%。The wax is preferably added in an amount of from 5 to 30% by weight, and more preferably from 5 to 20% by weight, based on the weight of the second resin layer.
該用於本發明的聚乙烯樹脂較佳具有一自1至20克/10分鐘的熔化指數(MI),且可選自以下所組成的群組:低密度聚乙烯、直鏈低密度聚乙烯、直鏈超低密度聚乙烯、中密度聚乙烯、高密度聚乙烯、超高密度聚乙烯、主要含乙烯的共聚物、及其等之樹脂摻合物。較佳有用的聚乙烯樹脂為高密度聚乙烯樹脂。The polyethylene resin used in the present invention preferably has a melt index (MI) of from 1 to 20 g/10 minutes, and may be selected from the group consisting of low density polyethylene, linear low density polyethylene. , linear ultra-low density polyethylene, medium density polyethylene, high density polyethylene, ultra high density polyethylene, copolymer mainly containing ethylene, and resin blends thereof. A preferred useful polyethylene resin is a high density polyethylene resin.
該第二樹脂層可進一步包含一α-晶體成核劑。一旦冷卻呈熔態之該聚乙烯時,該α-晶體成核劑可作為晶體 成長的晶核,因此可快速地形成晶體,藉此產生許多小且均勻的晶體。以100重量份該聚乙烯樹脂計,該α-晶體成核劑之添加量較佳可以是0.0001至5重量份,且更佳為0.001至1重量份。該α-晶體成核劑可選自以下所組成的群組:二亞苄山梨糖醇;羧酸,其包括脂肪族羧酸、脂環族羧酸、芳香族羧酸等;脂肪族醯胺;無機顆粒,其包括氧化矽、滑石、高嶺土、碳化鈣等;甘油;高碳脂肪酸酯,諸如甘油單酯等;及其等之混合物。The second resin layer may further comprise an α-crystal nucleating agent. The α-crystal nucleating agent can be used as a crystal once the polyethylene is melted in a molten state. The growing nucleus, so that crystals can be formed quickly, thereby producing many small and uniform crystals. The α-crystal nucleating agent may preferably be added in an amount of 0.0001 to 5 parts by weight, and more preferably 0.001 to 1 part by weight, based on 100 parts by weight of the polyethylene resin. The α-crystal nucleating agent may be selected from the group consisting of dibenzylidene sorbitol; a carboxylic acid comprising an aliphatic carboxylic acid, an alicyclic carboxylic acid, an aromatic carboxylic acid, etc.; an aliphatic guanamine Inorganic particles, including cerium oxide, talc, kaolin, calcium carbide, etc.; glycerin; high carbon fatty acid esters such as monoglycerides; and the like.
根據本發明之該積層多孔膜具有2或多層,例如2至5層。The laminated porous film according to the present invention has 2 or more layers, for example, 2 to 5 layers.
下文為根據本發明之一用於製造該積層多孔膜的方法之說明文。The following is a description of a method for producing the laminated porous film according to one of the present inventions.
該根據本發明的積層多孔膜係藉以下步驟而製成:a)添加一聚丙烯樹脂及一β-晶體成核劑,並使其等經熔態揑揉,藉此製成第一樹脂;b)添加一聚乙烯樹脂及具有90℃或更高的熔點及80%或更高之結晶度之蠟,並使其等經揑揉,因此製成第二樹脂;c)分別擠製該第一樹脂及第二樹脂,且使其等進行積層化,藉此形成一含經積層之第一樹脂層及第二樹脂層的非拉製薄片;及d)拉製該非拉製薄片。The laminated porous film according to the present invention is produced by the following steps: a) adding a polypropylene resin and a β-crystal nucleating agent, and kneading them in a molten state, thereby preparing a first resin; b) adding a polyethylene resin and a wax having a melting point of 90 ° C or higher and a crystallinity of 80% or higher, and kneading the same, thereby preparing a second resin; c) separately extruding the first a resin and a second resin are laminated to form a non-drawn sheet comprising the laminated first resin layer and the second resin layer; and d) the non-drawn sheet is drawn.
明確地說,在步驟a)內,係添加100重量份一具有熔化指數為1至20克/10分鐘的聚丙烯樹脂、以及0.0001至5重量份一β-晶體成核劑(例如N,N’-二環己基-2,6-奈二羧醯胺),然後使其等經熔化揑揉,藉此製成一第一樹脂。因 此,該熔化揑揉溫度較佳設定於250℃或較低,例如200至230℃,且冷卻並粒化所製成之該第一樹脂。Specifically, in the step a), 100 parts by weight of a polypropylene resin having a melt index of 1 to 20 g/10 minutes, and 0.0001 to 5 parts by weight of a β-crystal nucleating agent (for example, N, N) are added. '-Dicyclohexyl-2,6-naphthylcarboxamide), which is then melted and kneaded to thereby form a first resin. because Thus, the melt kneading temperature is preferably set at 250 ° C or lower, for example, 200 to 230 ° C, and the first resin produced is cooled and granulated.
在步驟b)內,係添加一具有熔化指數為1至20克/10分鐘的聚乙烯樹脂、及具有熔點為90℃或更高及結晶度為80%或更高的蠟、以及一α-晶體成核劑,然後使其等經熔化揑揉,藉此製成一第二樹脂。該熔化揑揉溫度較佳設定於230℃或較低,例如180至220℃,並冷卻且粒化所製成之該第二樹脂。In the step b), a polyethylene resin having a melt index of 1 to 20 g/10 minutes, and a wax having a melting point of 90 ° C or higher and a crystallinity of 80% or higher, and an α- are added. The crystal nucleating agent is then subjected to melt kneading to thereby form a second resin. The melted kneading temperature is preferably set at 230 ° C or lower, for example, 180 to 220 ° C, and the second resin produced is cooled and granulated.
在步驟c)內,係分別使步驟a)及b)內所製成的第一樹脂及第二樹脂經熔化揑揉且冷卻以便使用一鑄軋輥進行鑄造,藉此獲得一含積層之第一及第二樹脂層的非拉製薄片。該熔化擠裝溫度較佳設定於小於250℃,例如200至230℃,且該鑄軋輥的溫度較佳設定至100℃或更低,例如110至130℃。In the step c), the first resin and the second resin produced in the steps a) and b) are respectively melted and kneaded and cooled to be cast using a casting roll, thereby obtaining a first layer containing a layer. And a non-drawn sheet of the second resin layer. The melt extrusion temperature is preferably set to less than 250 ° C, for example, 200 to 230 ° C, and the temperature of the casting roll is preferably set to 100 ° C or lower, for example, 110 to 130 ° C.
在步驟d)內,係連續雙軸向拉製步驟c)內所獲得的積層薄片以形成一薄膜。可以在90℃或更高的溫度範圍內,以2至10倍的抽拉比及縱向(MD)及橫向(TD)中之各方向進行該拉製法。若該拉製溫度小於90℃,則會增加崩潰性能,且膜形成安定性會變得明顯有問題。因此,在根據本發明之該方法中的拉製溫度較佳設定至不會超過該第二樹脂內所含之蠟的熔點之溫度,亦即90℃或更高,例如90℃或更高。例如該積層薄片係於95℃下以2至10倍的抽拉比經拉製,然後於100℃下以TD及2至10倍的抽拉比經拉製,藉以形成一所欲薄膜。In step d), the laminated sheets obtained in step c) are continuously biaxially drawn to form a film. The drawing method can be carried out in a drawing ratio of 2 to 10 times and a direction in the machine direction (MD) and the transverse direction (TD) in a temperature range of 90 ° C or higher. If the drawing temperature is less than 90 ° C, the collapse property is increased, and the film formation stability becomes apparently problematic. Therefore, the drawing temperature in the method according to the present invention is preferably set to a temperature which does not exceed the melting point of the wax contained in the second resin, that is, 90 ° C or higher, for example, 90 ° C or higher. For example, the laminated sheet is drawn at a draw ratio of 2 to 10 times at 95 ° C, and then drawn at 100 ° C and a draw ratio of 2 to 10 times at 100 ° C to form a desired film.
藉此獲得之該積層多孔膜可以於100℃或更高的溫度下經熱處理,藉此得到尺寸安定性。The laminated porous film thus obtained can be subjected to heat treatment at a temperature of 100 ° C or higher, thereby obtaining dimensional stability.
根據本發明之該積層多孔膜可顯示小於或等於500秒/100毫升之25℃葛利(Gurley)透氣性,其係指根據ASTM D726,於25℃下使100毫升空氣通過一具有645毫米2 之面積之薄膜所需的時間。The laminated porous film according to the present invention may exhibit a 25 ° C Gurley gas permeability of 500 sec/100 ml or less, which means that 100 ml of air is passed through a 645 mm 2 at 25 ° C according to ASTM D726. The time required for the film of the area.
而且,於135℃下加熱30秒後,根據本發明之該積層多孔膜可顯示大於40,000秒/100毫升之葛利透氣性,其係指根據ASTM D726,於135℃下在一烘箱內經熱處理30秒後,使100毫升空氣通過一具有645毫米2 面積的薄膜所需之時間。因此,根據本發明之該薄膜可顯示優異的斷開性質。Moreover, after heating at 135 ° C for 30 seconds, the laminated porous film according to the present invention can exhibit a Gurley gas permeability of more than 40,000 sec / 100 ml, which means heat treatment in an oven at 135 ° C according to ASTM D726 30 After a second, 100 ml of air was passed through a film having a 645 mm 2 area for the time required. Therefore, the film according to the present invention can exhibit excellent breaking properties.
根據本發明之該多孔聚丙烯膜可具有優異的崩潰及斷開性質、以及高透氣性,因此可有效率地施用於二次電池等之隔離件。The porous polypropylene film according to the present invention can have excellent collapse and breakage properties as well as high gas permeability, and thus can be efficiently applied to a separator of a secondary battery or the like.
因此,本發明提供一用於含該積層多孔膜之二次電池的隔離件。該二次電池較佳為鋰二次電池。Accordingly, the present invention provides a separator for a secondary battery including the laminated porous film. The secondary battery is preferably a lithium secondary battery.
根據本發明之該積層多孔膜較佳具有10至50微米的總厚度,因此可用於一適於二次電池的隔離件中。The laminated porous film according to the present invention preferably has a total thickness of 10 to 50 μm, and thus can be used in a separator suitable for a secondary battery.
下文,係藉以下實例而更詳細描述本發明,但是其等僅用於闡明,並無意限制本發明。In the following, the invention is described in more detail by the following examples, which are intended to illustrate and not to limit the invention.
添加100重量份之聚丙烯樹脂(MI:3.0克/10分鐘)、與0.2重量份作為β-晶體成核劑之N,N’-二環己基-2,6-萘二羧醯胺,藉此製成一聚丙烯樹脂組成物,然後於220℃下使其經熔化揑揉,並於室溫下冷卻且粒化,藉以製造薄片A。100 parts by weight of a polypropylene resin (MI: 3.0 g/10 min), and 0.2 part by weight of N,N'-dicyclohexyl-2,6-naphthalenedicarbamide as a β-crystal nucleating agent were added. This was made into a polypropylene resin composition, which was then kneaded by melting at 220 ° C, and cooled and granulated at room temperature to thereby produce a sheet A.
此外,添加100重量份聚乙烯樹脂(MI 5.5克/10分鐘)、及10重量份具有91℃熔點及85%結晶度的微晶狀蠟、與0.3重量份α-晶體成核劑,藉此製成一聚乙烯樹脂組成物,然後於220。℃下使其經熔化揑揉,並於室溫下冷卻且粒化,藉以製造薄片B。Further, 100 parts by weight of a polyethylene resin (MI 5.5 g/10 min), and 10 parts by weight of a microcrystalline wax having a melting point of 91 ° C and 85% crystallinity, and 0.3 part by weight of an α-crystal nucleating agent are added, whereby A polyethylene resin composition was formed and then at 220. It was kneaded by melting at ° C, and cooled and granulated at room temperature to thereby produce a sheet B.
於220℃下使用一熔態擠製機將該等薄片A及B分別熔態擠製成一層A及層B,其後使用一進料裝置使這些層體積層成為一種三層結構(A/B/A=3:1:3厚度比),且冷卻以便於120℃下使用一鑄軋輥進行鑄製,藉此製成一積層薄片。The sheets A and B were respectively melted into a layer A and a layer B at 220 ° C using a melt extruder, and then the layer layers were made into a three-layer structure using a feeding device (A/). B/A = 3:1:3 thickness ratio), and cooled to be cast at 120 ° C using a casting roll, thereby forming a laminated sheet.
於95℃下以MD及4倍之抽拉比拉製該積層薄片,然後於100℃下以TD及3倍之抽拉比進行拉製,藉此製成一積層多孔膜。The laminated sheet was drawn at a draw ratio of MD and 4 times at 95 ° C, and then drawn at a drawing ratio of TD and 3 times at 100 ° C to thereby form a laminated porous film.
除了使用具有101℃熔點及90%結晶度之微晶狀蠟製成該聚乙烯樹脂組成物不同外,以如同實例1的方法製造一積層多孔膜。A laminated porous film was produced in the same manner as in Example 1 except that the polyethylene resin composition was made using a microcrystalline wax having a melting point of 101 ° C and a crystallinity of 90%.
除了使用具有116℃熔點及92%結晶度之微晶狀 蠟製成該聚乙烯樹脂組成物不同外,以如同實例1的方法製造一積層多孔膜。In addition to using a microcrystalline crystal having a melting point of 116 ° C and 92% crystallinity A laminated porous film was produced in the same manner as in Example 1 except that the wax was made into the polyethylene resin composition.
除了使用具有128℃熔點及87%結晶度之微晶狀蠟製成該聚乙烯樹脂組成物不同外,以如同實例1的方法製造一積層多孔膜。A laminated porous film was produced in the same manner as in Example 1 except that the polyethylene resin composition was made using a microcrystalline wax having a melting point of 128 ° C and 87% crystallinity.
除了使用具有84℃熔點及87%結晶度的微晶狀蠟製成該聚乙烯樹脂組成物不同外,以如實例1的方法製造一積層多孔膜。A laminated porous film was produced in the same manner as in Example 1 except that the polyethylene resin composition was made using a microcrystalline wax having a melting point of 84 ° C and 87% crystallinity.
除了使用具有109℃熔點及65%結晶度的微晶狀蠟製成該聚乙烯樹脂組成物不同外,以如實例1的方法製造一積層多孔膜。A laminated porous film was produced in the same manner as in Example 1 except that the polyethylene resin composition was made using a microcrystalline wax having a melting point of 109 ° C and a crystallinity of 65%.
實例1至4、及比較例1及2內所製成之該等薄膜的性能之評估如下。結果示於下表1內。The properties of the films prepared in Examples 1 to 4 and Comparative Examples 1 and 2 were evaluated as follows. The results are shown in Table 1 below.
根據ASTM D726,使用一葛利型密度計(G-B3C Toyoseiki),於25℃下測定使100毫升空氣通過一具有645毫米2 的面積之薄膜所需的時間。The time required to pass 100 ml of air through a film having an area of 645 mm 2 was measured at 25 ° C according to ASTM D726 using a Gurley Densitometer (G-B3C Toyoseiki).
於135℃下在一烘箱內經熱處理30秒後,根據ASTM D726,使用一葛利型密度計(G-B3C Toyoseiki),測定使100毫升空氣通過一具有645毫米2 之面積的薄膜所需 的時間,並評估斷開(SD)性質。After heat treatment in an oven for 30 seconds at 135 ° C, the time required to pass 100 ml of air through a film having an area of 645 mm 2 was measured according to ASTM D726 using a G-B3C Toyoseiki. And evaluate the nature of disconnection (SD).
如自表1所知,實例及比較例之所有薄膜顯示有效的斷開(SD)性能。然而,僅使用該具有90℃或更高之熔點及80%或更高之結晶度的蠟之實例1至4的薄膜顯示適用於隔離件的透氣性。As understood from Table 1, all of the films of the examples and comparative examples showed effective disconnection (SD) performance. However, the films of Examples 1 to 4 using only the wax having a melting point of 90 ° C or higher and a crystallinity of 80% or higher showed suitability for the gas permeability of the separator.
雖然本發明業經參考上述特定實施例加以說明,但是應該瞭解藉熟悉本項技藝者而進行之本發明的各種修飾及改變亦屬於如附加申請專利範圍所定義的本發明範圍。Although the present invention has been described with reference to the specific embodiments thereof, it is to be understood that the various modifications and changes of the present invention as defined by the appended claims.
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