WO1997020883A1 - Microporous polyethylene membranes having low fusing temperatures - Google Patents
Microporous polyethylene membranes having low fusing temperatures Download PDFInfo
- Publication number
- WO1997020883A1 WO1997020883A1 PCT/JP1996/003560 JP9603560W WO9720883A1 WO 1997020883 A1 WO1997020883 A1 WO 1997020883A1 JP 9603560 W JP9603560 W JP 9603560W WO 9720883 A1 WO9720883 A1 WO 9720883A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- polyethylene
- unit content
- microporous
- membrane
- mol
- Prior art date
Links
Classifications
-
- 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
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/26—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof by elimination of a solid phase from a macromolecular composition or article, e.g. leaching out
-
- 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
-
- 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
- H01M50/489—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
- H01M2200/00—Safety devices for primary or secondary batteries
- H01M2200/10—Temperature sensitive devices
-
- 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
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S428/00—Stock material or miscellaneous articles
- Y10S428/913—Material designed to be responsive to temperature, light, moisture
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/249921—Web or sheet containing structurally defined element or component
- Y10T428/249953—Composite having voids in a component [e.g., porous, cellular, etc.]
- Y10T428/249978—Voids specified as micro
Definitions
- the present invention relates to a microporous polyethylene membrane, a separator comprising the same, and a battery using the same as a battery separator.
- microporous membranes are used for microfiltration membranes, separators for batteries, separators for capacitors, etc.
- microporous polyethylene membranes when used as separators for batteries, especially for lithium ion batteries, microporous polyethylene membranes have general physical properties such as membrane mechanical strength and permeability.
- the separator melts to form a film covering the electrodes and cuts off the current to ensure the safety of the battery. It has been demanded.
- the fuse temperature that is, the temperature at which the fuse effect occurs
- the microporous film melts and covers the electrode as a film when the fuse temperature is reached, so that the flow of ions is interrupted and the battery reaction stops.
- the temperature rises extremely sharply the temperature inside the battery rises even after the fuse is blown, and as a result, the film may be broken and a short may occur in the battery.
- Development of a low-polyethylene microporous membrane has been an issue.
- JP-A-5-250305 and JP-A-2-2-15959 include ultra-high molecular weight polyethylene (UHMWPE), branched low-density polyethylene (LDPE) or linear low-density polyethylene.
- UHMWPE ultra-high molecular weight polyethylene
- LDPE branched low-density polyethylene
- LLDPE linear low-density polyethylene
- Ml melt index
- An object of the present invention is to solve the above-mentioned problems and to provide a microporous polyethylene membrane having excellent mechanical strength, permeability and productivity, and having a low fuse temperature.
- the present inventors have studied a linear copolymerized polyethylene having a much higher molecular weight than LLDPE used in the prior art.
- the linear copolymerized polyethylene can be made porous even when used alone, and the microporous polyethylene membrane produced therefrom has a high strength and a low fuse temperature comparable to those of the prior art. I found it.
- such membranes did not have sufficient permeability to be used as a separator when compared to membranes made from high molecular weight HDPE.
- the microporous membrane made of force is composed of a linear copolymerized polyethylene (hereinafter also referred to as C4 copolymer) using butene-11 as a comonomer or a copolymer using other ⁇ -olefin olefin.
- C4 copolymer a linear copolymerized polyethylene
- the present inventors have found that shrinkage is smaller than that of a membrane and that the membrane has sufficient permeability to be used as a separator.
- C3 copolymers specifically cause high porosity in the membrane, but the methyl groups, which are the side chains of C3 copolymers, are more likely to be incorporated into the polymer crystals than the ethyl and butyl groups.
- the C3 copolymer was a copolymer, it had a crystal structure closer to HDP II, and could exhibit higher permeability than a copolymer using other comonomers such as C4 copolymer. It is considered possible.
- the present inventors have conducted intensive studies to achieve higher permeability, and as a result, instead of using the C3 copolymer alone, when used as a mixture with high-density polyethylene, higher permeability was obtained at the same fuse temperature. Battery, and based on this knowledge, succeeded in producing a battery with further improved discharge characteristics and safety. did.
- a first aspect of the present invention is a linear copolymer polyethylene having a melt index of less than 0.1 and a propylene unit content of 0.1 to 4 mol%, and a fuse temperature of less than 13 ° C. It is a polyethylene microporous membrane.
- a linear copolymerized polyethylene having a melt index of less than 0.1, a propylene unit content of 0.1 to 4 mol% and a high-density polyethylene having a comonomer unit content of less than 0.1 mol%.
- the mixture has a weight average molecular weight of 25 to 700,000, a propylene unit content of 0.1 to 4 mol%, and a fuse temperature of 1 36 °. It is a polyethylene microporous membrane having a value of less than C
- a third aspect of the present invention is a separator comprising the above-described polyethylene microporous membrane.
- a fourth aspect of the present invention is a battery using the above separator as a separator for a battery.
- the melt index (Ml) of the C3 copolymer and the mixture of C3 copolymer and high density polyethylene is less than 0.1, preferably less than 0.07, more preferably less than 0.05. If MI is 0.1 or more, it is difficult to make the membrane porous.
- the C3 copolymer having such MI and the above-mentioned mixture have a weight average molecular weight.
- its weight average molecular weight is from 200,000 to 700,000, preferably from 250,000 to 600,000, and more preferably from 250,000 to 500,000.
- the propylene unit content of the C3 copolymer is 0.1 to 4 mol%, preferably 0.2 to 3 mol%, more preferably 0.5 to 2 mol%, based on ethylene units. If the propylene unit content is less than 0.1 mol% with respect to the ethylene unit, the fuse temperature will be insufficiently reduced. If it exceeds 4 mol%, the crystallinity will be excessively reduced, making it difficult to make the film porous.
- the density of the C3 copolymer is from 0.85 to 0.97, preferably from 0.90 to 0.96, and more preferably from 0.92 to 0.95.
- the C3 copolymer used in the present invention can be produced by various known methods, for example, a chromium compound-supported catalyst or a magnesium compound-containing powder as disclosed in JPB-1-127777. It can be produced by polymerization using a catalyst.
- the C3 copolymer is used alone by mixing the C3 copolymer with a high-density polyethylene having a comonomer unit content of less than 0.1 mol% (hereinafter, also referred to as HDPE).
- a high-density polyethylene having a comonomer unit content of less than 0.1 mol% hereinafter, also referred to as HDPE.
- the relationship between permeability and fuse temperature can be further improved.
- the weight average molecular weight of the mixable HDPE is from 100,000 to 400,000, preferably from 200,000 to 100,000, and more preferably from 250,000 to 700,000.
- the proportion of C3 copolymer in the mixture is between 1% and 100%, preferably between 5% and 90%, more preferably between 10% and 80%. If the proportion of the C 3 copolymer is less than 1%, it is difficult to obtain a sufficiently low L and fuse temperature.
- the weight average molecular weight of the mixture is from 250,000 to 700,000, preferably from 250,000 to 700,000, and more preferably from 250,000 to 500,000.
- the propylene unit content of the C3 copolymer can be selected from the range of 0.1 to 4.0 mol%, but in view of dilution with HDPE, the propylene unit content is higher than when used alone. It is preferable to set to.
- the polyethylene microporous membrane is prepared by dissolving polyethylene in a solvent called a plasticizer at a temperature equal to or higher than its melting point, and cooling the resulting solution to a temperature lower than a crystallization temperature to form a polymer gel.
- the film is formed using (film forming step), and the obtained film is stretched. After (stretching step), the plasticizer is removed (plasticizer removing step).
- the plasticizer as used herein means an organic compound capable of forming a uniform solution with polyethylene at a temperature lower than its boiling point. Specific examples thereof include decalin, xylene, octyl phthalate, dibutyl phthalate, stearyl alcohol, and oleyl alcohol. , Decyl alcohol, nonyl alcohol, diphenyl ether, n-decane, n-dodecane, paraffin oil and the like. Of these, paraffin oil, dioctyl phthalate and decalin are preferred.
- the ratio of the plasticizer in the polymer gel is not particularly limited, it is 20% to 90%, preferably 50% to 70%. If the ratio of the plasticizer is less than 20%, it is difficult to obtain a microporous film having an appropriate porosity. If the ratio is more than 90%, the viscosity of the hot solution is lowered, and continuous molding of the sheet becomes difficult.
- the film forming method is not particularly limited.
- a linear copolymer polyethylene powder and a plasticizer are supplied to an extruder, and the both are melt-kneaded at a temperature of about 200 ° C., and then a usual hanger coat die is used.
- a sheet having a film thickness of several tens of meters to several mm can be continuously formed.
- ultra-high molecular weight polyethylene is not used as an essential component, so no special heating and melting equipment is required, and it is extremely simple simply by adding polyethylene and a plasticizer to the extruder. A highly homogeneous sheet can be prepared.
- the stretching method is not particularly limited, but a tenter method, a roll method, a rolling method, or the like can be used. Of these, simultaneous biaxial stretching by the ten-and-one method is preferred.
- the stretching temperature is a temperature from room temperature to the melting point of the polymer gel, preferably 80 to 130 ° C, more preferably 100 to 125 ° C.
- the stretching ratio is 4 to 400 times, preferably 8 to 200 times, more preferably 16 to 100 times, as a ratio depending on the area. Stretch ratio If it is 4 times or less, the strength as a separator is insufficient, and if it is 400 times or more, not only stretching is difficult, but also adverse effects such as low porosity of the obtained microporous membrane are likely to occur.
- a microporous film is obtained by removing a plasticizer from the stretched film.
- the method for removing the plasticizer is not particularly limited.
- paraffin oil dioctyl sulfate when used as a plasticizer, these may be extracted with an organic solvent such as methylene chloride-methyl ethyl ketone. By heating and drying at the temperature described above, it can be more sufficiently removed.
- a low-boiling compound such as decalin
- it can be removed only by heating and drying at a temperature lower than the fuse temperature of the microporous film.
- the polyethylene microporous film obtained by the above-described manufacturing method is subjected to a heat treatment at a temperature lower than the fuse temperature as necessary.
- the thickness of the microporous membrane is 1 to 5005111, preferably 10 to 200 ⁇ 111, and more preferably 15 to 50 ⁇ . If the film thickness is smaller than 1 m, the mechanical strength of the film is not sufficient, and if it is larger than 500 // m, there is a problem in reducing the size and weight of the battery.
- methylene chloride is used in the present invention at room temperature in an unconstrained state. It is evaluated by the numerical value when the plasticizer is removed by extraction.
- the porosity at 2 hours is 20 to 80%, preferably 35 to 50%. If the porosity is less than 20%, the permeability is not sufficient, and if the porosity is more than 80%, sufficient mechanical strength cannot be obtained.
- the air permeability in the present invention is from 10 seconds to 6,000 seconds, preferably from 50 seconds to 4,000 seconds, and more preferably from 100 seconds to 2,000 seconds. If the air permeability is more than 600 seconds, the permeability is not sufficient, and if the air permeability is less than 10 seconds, the pore size becomes large. It is not preferable because it breaks.
- the pore diameter of the pores in the microporous membrane is from 0.001 to 0.3 m, preferably from 0.05 to 0.1 m, more preferably from 0.01 to 0.05 m. If the pore size is less than 0.001 ⁇ m, the permeability is not sufficient, and if the pore size is more than 0.3 ⁇ m, not only the occurrence of current interruption due to the fuse effect is delayed, but also the deposited dendrites and the collapsed activities A membrane having such pores is not suitable for use as a battery separator due to concerns about a short circuit caused by a substance.
- test method for the properties shown in the examples is as follows.
- the measurement was performed using a dial gauge (Ozaki Seisakusho: PEACOCK No.25).
- a 20 cm square sample was cut out from the microporous membrane, the volume and weight were determined, and the obtained result was calculated using the following equation.
- the molar equivalent (A) of the integrated value of the signal intensity derived from the comonomer unit is represented by (A) and the molar equivalent (B) of the integrated value of the signal intensity derived from the ethylene unit. Calculate the quotient obtained by dividing by the sum of 100 and multiply by 100 to obtain the unit content of comonomer (mo 1%).
- melt index measured at a temperature of 190 C and a load of 2.16 kg was defined as MI. If the MI is sufficiently smaller than 0.1 and less than about 0.0i, the measurement of the MI tends to vary. (Load 2.16 k) and HM I measured at a load of 21.6 kg can be used. (8) Fuse temperature
- the electrolyte is impregnated into a microporous polyethylene membrane cut to a thickness of 20 mm, the membrane is sandwiched between two nickel electrodes at a pressure of 20 kgcm, and the temperature is raised from room temperature at 20 ° C / min. Was measured under the conditions of 1 V and 1 kHz. In this measurement, the temperature at which the impedance reached 1,000 ⁇ was defined as the fuse temperature.
- a lithium-ion battery was manufactured using an electrolyte prepared by adding lithium borofluoride to a lithium ion battery. After charging this battery at 4.2 V for 5 hours, it was overcharged with a constant current. Overcharging raises the battery's internal temperature and shuts off current when the sample's fuse temperature is reached. Thereafter, a sample in which current recovery did not occur for 10 minutes or more was evaluated as ⁇ . Since this test was an accelerated test, the test was performed with safety devices such as PTC elements mounted on the actual battery removed.
- Example 3 (Invention)
- a microporous polyethylene membrane was prepared in the same manner as in 1. Table 1 shows the physical properties of the obtained film.
- Example 1 with the exception of using a C3 copolymer with a MI of less than 0.01, a HM I of 0.65 and a weight average molecular weight of 480,000 (density 933, propylene unit content 1.6 mol%, but measured by IR spectrum)
- a microporous polyethylene membrane was prepared in the same manner as described above. Table 1 shows the physical properties of the obtained film.
- Example 1 except that a C3 copolymer with an IMI of less than 0.01, an HMI of 0.46, and a weight average molecular weight of 520,000 (density 0.929, propylene unit content 1.9 mol%, as measured by IR spectrum) was used.
- a microporous polyethylene membrane was prepared in the same manner as described above. Table 1 shows the physical properties of the obtained film.
- Example 7 (comparison) MI 0.01 3. HM I 0.54 and the same method as in Example 1 except that a C4 copolymer having a weight average molecular weight of 400,000 (density: 928, butene unit content: 1.3 mol%) was used. Produced a microporous polyethylene membrane. Table 1 shows the physical properties of the obtained film.
- Example 2 The same method as in Example 1 was tried except that extraction was performed under constraint using LLDPE (density 0.99.17) of MI 0.4, but the appearance of the membrane was transparent and the microporous membrane was Not obtained.
- LLDPE density 0.99.17
- Example 2 The same method as in Example 1 was tried except that 40 parts of LDPE (density 0.99.17) of MI 0.3 and 60 parts of paraffin oil (Matsumura Oil: P350P) were used. The strength was too low to stretch.
- the HMI was 43 and the propylene unit content was 0.5 mol% (measured by IR spectrum).
- Table 2 shows the physical properties of the obtained film.
- a polyethylene microporous membrane was prepared in the same manner as in Example 1 except that the stretching temperature was set to 120 ° C. Using the obtained membrane, the melt index (HMI) and the propylene unit content of the polyethylene were measured. As a result, the HMI was 1.46 and the propylene unit content was 0.8 mol% (IR spectrum). Was measured). Table 2 shows the physical properties of the obtained film.
- a microporous polyethylene membrane was prepared in the same manner as in Example 1 except that the above procedure was adopted. Using the obtained membrane, the melt index (HMI) and the propylene unit content of the polyethylene were measured. As a result, the HMI was 0.96, and the propylene unit content was 0.9 mol% (IR spectrum). Was measured). Table 2 shows the physical properties of the obtained film.
- High-density polyethylene with a weight average molecular weight of 250,000 (density 9556, comonomer unit content 0.0 mol%) 20 parts, MLD 0.4 LLDPE (density 0.917) 20 parts, paraffin Oil (Matsumura Petroleum Institute: P350P)
- the same method as in Example 1 was tried except that 60 parts were used and the stretching temperature was set to 120 ° C, but the obtained film was transparent. There was no microporous membrane.
- High-density polyethylene having a weight average molecular weight of 250,000 (density 0.956, comonomer unit content 0.0 mol%) 20 parts, LDPE with Ml 0.3 (density 0.917) 20 parts, paraffin oil (Matsumura Petroleum Research Institute: P350P)
- the same method as in Example 1 was used except that 60 parts were used and the stretching temperature was set to 120 ° C.
- the obtained film was transparent, No microporous membrane was obtained.
- Example 1 Example 2 Example 3 Example 4 Example 5 Example 7 Example 8 Example 9 Example 10
- Example 17 (honhon) (hon-hon (hon-hon) (hon-hon (hon-na (hi-nori) (hi-ho))
- the microporous polyethylene membrane of the present invention has excellent mechanical strength, permeability, and productivity, and has a low fuse temperature. Therefore, when used as a separator for batteries such as lithium ion batteries, a highly reliable battery can be manufactured. can do.
Description
Claims
Priority Applications (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/077,943 US6168858B1 (en) | 1995-12-05 | 1996-12-05 | Microporous polyethylene membranes having low fusing temperatures |
JP09521160A JP3113287B2 (ja) | 1995-12-05 | 1996-12-05 | 低いヒューズ温度を有するポリエチレン微多孔膜 |
CA002239449A CA2239449C (en) | 1995-12-05 | 1996-12-05 | Polyethylene microporous film having low fusing temperature |
KR1019980704189A KR100257359B1 (ko) | 1995-12-05 | 1996-12-05 | 낮은 융합 온도를 갖는 미세다공성 폴리에틸렌 막 |
AU10408/97A AU1040897A (en) | 1995-12-05 | 1996-12-05 | Microporous polyethylene membranes having low fusing temperatures |
EP96941175A EP0877046B1 (en) | 1995-12-05 | 1996-12-05 | Microporous polyethylene membranes having low fusing temperatures |
DE69636348T DE69636348T2 (de) | 1995-12-05 | 1996-12-05 | Mikroporöse polyethylenmembran mit niedriger schmelztemperatur |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7/339851 | 1995-12-05 | ||
JP33985195 | 1995-12-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1997020883A1 true WO1997020883A1 (en) | 1997-06-12 |
Family
ID=18331429
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP1996/003560 WO1997020883A1 (en) | 1995-12-05 | 1996-12-05 | Microporous polyethylene membranes having low fusing temperatures |
Country Status (9)
Country | Link |
---|---|
US (1) | US6168858B1 (ja) |
EP (1) | EP0877046B1 (ja) |
JP (1) | JP3113287B2 (ja) |
KR (1) | KR100257359B1 (ja) |
AU (1) | AU1040897A (ja) |
CA (1) | CA2239449C (ja) |
DE (1) | DE69636348T2 (ja) |
TW (1) | TW460516B (ja) |
WO (1) | WO1997020883A1 (ja) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH11279324A (ja) * | 1998-03-30 | 1999-10-12 | Asahi Chem Ind Co Ltd | ポリエチレン微多孔膜 |
US6096213A (en) * | 1998-08-14 | 2000-08-01 | 3M Innovative Properties Company | Puncture-resistant polyolefin membranes |
JP2002338730A (ja) * | 2001-05-18 | 2002-11-27 | Asahi Kasei Corp | ポリエチレン製微多孔膜及びそれを用いた電池 |
WO2004085525A1 (ja) * | 2003-03-24 | 2004-10-07 | Asahi Kasei Chemicals Corporation | ポリエチレン微多孔膜 |
CN100334144C (zh) * | 2003-03-24 | 2007-08-29 | 旭化成化学株式会社 | 聚乙烯微多孔膜 |
US8104625B2 (en) | 2004-05-20 | 2012-01-31 | Asahi Kasei Chemicals Corporation | Microporous membrane made of polyolefins |
JP2021102744A (ja) * | 2019-12-24 | 2021-07-15 | ハンファ トータル ペトロケミカル カンパニー リミテッド | ポリエチレン樹脂組成物およびこれから製造された二次電池用分離膜 |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20030158313A1 (en) * | 2003-03-12 | 2003-08-21 | Spicher Dennis R. | Antistatic additives including tetrahalogenated ionic compounds for organic polymer packaging compositions |
US7267909B2 (en) * | 2003-06-06 | 2007-09-11 | Amtek Research International Llc | Battery separators containing reactive functional groups |
US7361247B2 (en) * | 2003-12-31 | 2008-04-22 | Neenah Paper Inc. | Matched heat transfer materials and method of use thereof |
US20080193833A1 (en) | 2004-10-01 | 2008-08-14 | Asahi Kasei Kabushiki Kaisha | Polyolefin Microporous Membrane |
DE102006014360A1 (de) * | 2005-03-30 | 2006-12-07 | Sumitomo Chemical Co., Ltd. | Poröser Film und Herstellungsverfahren und Anwendungen desselben |
US9091005B2 (en) * | 2006-02-24 | 2015-07-28 | Mitsui Chemicals, Inc. | Nonwoven web for fastener female member |
US7981536B2 (en) * | 2006-08-31 | 2011-07-19 | Toray Tonen Specialty Separator Godo Kaisha | Microporous membrane, battery separator and battery |
US7807287B2 (en) * | 2006-08-31 | 2010-10-05 | Tonen Chemical Corporation | Multi-layer, microporous membrane, battery separator and battery |
ATE533197T1 (de) † | 2006-09-20 | 2011-11-15 | Asahi Kasei Chemicals Corp | Mikroporöse polyolefinmembran und separator für batterie mit nichtwässrigem elektrolyt |
JP5034414B2 (ja) * | 2006-09-26 | 2012-09-26 | 住友化学株式会社 | 積層多孔性フィルムおよび非水電解質二次電池用セパレータ |
JP5195341B2 (ja) * | 2008-11-19 | 2013-05-08 | Tdk株式会社 | リチウムイオン二次電池用セパレータ及びリチウムイオン二次電池 |
EP4143139A4 (en) * | 2020-05-01 | 2024-05-15 | Celanese Int Corp | MEMBRANE WITH REDUCED SWITCH-OFF TEMPERATURE AND POLYMER COMPOSITION FOR ITS PRODUCTION |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0192243A (ja) * | 1987-06-25 | 1989-04-11 | Toray Ind Inc | ポリオレフイン微孔性膜の製造方法 |
JPH0693130A (ja) * | 1992-07-30 | 1994-04-05 | Asahi Chem Ind Co Ltd | ポリオレフィン微孔性多孔膜の製造方法 |
JPH06345893A (ja) * | 1993-06-08 | 1994-12-20 | Mitsubishi Kasei Corp | 多孔性フィルムまたはシート |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4331622A (en) * | 1978-08-01 | 1982-05-25 | Asahi Kasei Kogyo Kabushiki Kaisha | Method for manufacturing a microporous film having low electrical resistance and high durability |
US4650730A (en) * | 1985-05-16 | 1987-03-17 | W. R. Grace & Co. | Battery separator |
US5036148A (en) * | 1985-11-25 | 1991-07-30 | E. I. Du Pont De Nemours And Company | Production of substantially linear highly crystalline polyolefins |
DE3850905T2 (de) * | 1987-05-06 | 1994-12-01 | Mitsui Petrochemical Ind | Molekular orientiertes geformtes Gebilde aus Ethylen-alpha-olefin-copolymer mit ultrahohem Molekulargewicht. |
JPH0221559A (ja) | 1988-07-08 | 1990-01-24 | Nitto Denko Corp | 電池用セパレータとその製造法 |
US5248461A (en) * | 1989-01-13 | 1993-09-28 | Stamicarbon B.V. | Process of making microporous films of UHMWPE |
NL9100279A (nl) * | 1991-02-18 | 1992-09-16 | Stamicarbon | Microporeuze folie uit polyetheen en werkwijze voor de vervaardiging daarvan. |
JP2657434B2 (ja) | 1991-07-19 | 1997-09-24 | 東燃株式会社 | ポリエチレン微多孔膜、その製造方法及びそれを用いた電池用セパレータ |
US5240655A (en) * | 1991-12-20 | 1993-08-31 | W. R. Grace & Co.-Conn. | Process of making a battery separator |
JP3281086B2 (ja) * | 1992-11-19 | 2002-05-13 | 旭化成株式会社 | セパレーター用ポリオレフィン微孔性多孔膜 |
AT401520B (de) * | 1994-03-22 | 1996-09-25 | Danubia Petrochem Polymere | Metallocene und deren einsatz für die olefinpolymerisation |
JP3455285B2 (ja) | 1994-05-16 | 2003-10-14 | 三井化学株式会社 | 高分子量エチレン・α−オレフィン共重合体よりなる多孔性二軸配向フィルムおよびその用途 |
US5618642A (en) * | 1995-06-06 | 1997-04-08 | Daramic, Inc. | Battery separator with sodium sulfate |
-
1996
- 1996-12-05 DE DE69636348T patent/DE69636348T2/de not_active Expired - Lifetime
- 1996-12-05 US US09/077,943 patent/US6168858B1/en not_active Expired - Lifetime
- 1996-12-05 EP EP96941175A patent/EP0877046B1/en not_active Expired - Lifetime
- 1996-12-05 KR KR1019980704189A patent/KR100257359B1/ko not_active IP Right Cessation
- 1996-12-05 CA CA002239449A patent/CA2239449C/en not_active Expired - Lifetime
- 1996-12-05 AU AU10408/97A patent/AU1040897A/en not_active Abandoned
- 1996-12-05 TW TW085115015A patent/TW460516B/zh not_active IP Right Cessation
- 1996-12-05 JP JP09521160A patent/JP3113287B2/ja not_active Expired - Lifetime
- 1996-12-05 WO PCT/JP1996/003560 patent/WO1997020883A1/ja active IP Right Grant
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0192243A (ja) * | 1987-06-25 | 1989-04-11 | Toray Ind Inc | ポリオレフイン微孔性膜の製造方法 |
JPH0693130A (ja) * | 1992-07-30 | 1994-04-05 | Asahi Chem Ind Co Ltd | ポリオレフィン微孔性多孔膜の製造方法 |
JPH06345893A (ja) * | 1993-06-08 | 1994-12-20 | Mitsubishi Kasei Corp | 多孔性フィルムまたはシート |
Non-Patent Citations (1)
Title |
---|
See also references of EP0877046A4 * |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH11279324A (ja) * | 1998-03-30 | 1999-10-12 | Asahi Chem Ind Co Ltd | ポリエチレン微多孔膜 |
US6096213A (en) * | 1998-08-14 | 2000-08-01 | 3M Innovative Properties Company | Puncture-resistant polyolefin membranes |
JP2002338730A (ja) * | 2001-05-18 | 2002-11-27 | Asahi Kasei Corp | ポリエチレン製微多孔膜及びそれを用いた電池 |
WO2004085525A1 (ja) * | 2003-03-24 | 2004-10-07 | Asahi Kasei Chemicals Corporation | ポリエチレン微多孔膜 |
CN100334144C (zh) * | 2003-03-24 | 2007-08-29 | 旭化成化学株式会社 | 聚乙烯微多孔膜 |
US8104625B2 (en) | 2004-05-20 | 2012-01-31 | Asahi Kasei Chemicals Corporation | Microporous membrane made of polyolefins |
JP2021102744A (ja) * | 2019-12-24 | 2021-07-15 | ハンファ トータル ペトロケミカル カンパニー リミテッド | ポリエチレン樹脂組成物およびこれから製造された二次電池用分離膜 |
Also Published As
Publication number | Publication date |
---|---|
EP0877046B1 (en) | 2006-07-12 |
US6168858B1 (en) | 2001-01-02 |
DE69636348T2 (de) | 2007-07-05 |
KR19990071903A (ko) | 1999-09-27 |
EP0877046A4 (en) | 2004-06-30 |
DE69636348D1 (de) | 2006-08-24 |
AU1040897A (en) | 1997-06-27 |
TW460516B (en) | 2001-10-21 |
EP0877046A1 (en) | 1998-11-11 |
KR100257359B1 (ko) | 2000-05-15 |
JP3113287B2 (ja) | 2000-11-27 |
CA2239449C (en) | 2002-05-21 |
CA2239449A1 (en) | 1997-06-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO1997023554A1 (en) | Short circuit-resistant polyethylene microporous film | |
TWI393285B (zh) | 聚烯烴微多孔膜及其製法、以及電池用隔離材與電池 | |
JP5202826B2 (ja) | ポリエチレン微多孔膜及びその製造方法並びに電池用セパレータ | |
TWI402172B (zh) | 微多孔聚烯烴薄膜、其製法、電池隔離材及電池 | |
JP5453272B2 (ja) | 微多孔膜およびそのような膜を製造し使用する方法 | |
TWI444296B (zh) | 聚烯烴微多孔膜及其製法、以及電池用隔離材與電池 | |
JP5596768B2 (ja) | ポリエチレン微多孔膜及び電池用セパレータ | |
WO1997020883A1 (en) | Microporous polyethylene membranes having low fusing temperatures | |
JP5216327B2 (ja) | ポリオレフィン製微多孔膜 | |
JP4804079B2 (ja) | ポリオレフィン製微多孔膜 | |
WO1996027633A1 (en) | Microporous polyethylene film and process for producing the film | |
CN102869710B (zh) | 聚烯烃微多孔膜、电池用隔板和电池 | |
KR20090027207A (ko) | 폴리올레핀 미세 다공막, 그 제조 방법, 전지용 세퍼레이터및 전지 | |
JPWO2008069216A1 (ja) | ポリオレフィン製微多孔膜 | |
KR102344220B1 (ko) | 폴리올레핀제 미세 다공막 및 이의 제조 방법, 비수 전해액계 이차전지용 세퍼레이터, 및 비수 전해액계 이차전지 | |
JPWO2019163935A1 (ja) | 多孔性ポリオレフィンフィルム | |
JP2015208894A (ja) | ポリオレフィン製積層微多孔膜 | |
WO2020203901A1 (ja) | ポリオレフィン微多孔膜、電池用セパレータ、二次電池及びポリオレフィン微多孔膜の製造方法 | |
JP3682120B2 (ja) | 電池セパレーター用複合膜及び電池用セパレーター | |
JP3252016B2 (ja) | ポリオレフィン微孔性多孔膜の製造方法 | |
JP3669777B2 (ja) | ポリエチレン微多孔膜 | |
KR20220069831A (ko) | 폴리올레핀 미다공막, 전지용 세퍼레이터 및 이차 전지 | |
JPH09259858A (ja) | セパレーター用ポリエチレン微多孔膜及びその製造方法 | |
JP2021105166A (ja) | ポリオレフィン微多孔膜、及び二次電池 | |
JP2020164858A (ja) | ポリオレフィン製微多孔膜、電池用セパレータ、及び二次電池 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AU CA CN JP KR RU US |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE CH DE DK ES FI FR GB GR IE IT LU MC NL PT SE |
|
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 1996941175 Country of ref document: EP |
|
ENP | Entry into the national phase |
Ref document number: 2239449 Country of ref document: CA Ref country code: CA Ref document number: 2239449 Kind code of ref document: A Format of ref document f/p: F |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1019980704189 Country of ref document: KR |
|
WWE | Wipo information: entry into national phase |
Ref document number: 09077943 Country of ref document: US |
|
WWP | Wipo information: published in national office |
Ref document number: 1996941175 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: 1019980704189 Country of ref document: KR |
|
WWG | Wipo information: grant in national office |
Ref document number: 1019980704189 Country of ref document: KR |
|
WWG | Wipo information: grant in national office |
Ref document number: 1996941175 Country of ref document: EP |