Patent Application
20090170005
This invention relates to a microporous polyolefin membrane, a battery separator formed thereby and a battery, particularly to a microporous polyolefin membrane having an excellent balance of shutdown temperature and speed and meltdown properties, a battery separator formed thereby and a battery.
Microporous polyethylene membranes are mainly used for battery separators. Particularly lithium ion battery separators are required to have not only excellent mechanical properties and permeability, but also a property of closing pores in batteries by heat generated by the short-circuiting of external circuits, overcharging, etc. to stop battery reactions (shutdown properties), a property of preventing membranes from breaking when temperatures are elevated after shutdown (meltdown properties), etc.
As a method for improving the properties of a microporous polyethylene membrane, the optimization of starting material compositions, production conditions, etc. has been proposed. For instance, Japanese Patent 2132327 proposes a microporous polyolefin membrane having excellent strength and permeability, which is made of a polyolefin composition comprising 1% or more by weight of ultra-high-molecular-weight polyolefin having a mass-average molecular weight (Mw) of 7×105 or more, and having a molecular weight distribution [mass-average molecular weight/number-average molecular weight (Mw/Mn)] of 10 to 300, the microporous polyolefin membrane having porosity of 35 to 95%, an average pore diameter of 0.001 to 0.2 μm, and a rupture strength of 0.2 kg or more per 15-mm width.
JP 2004-196870 A proposes a microporous polyolefin membrane comprising polyethylene, and polypropylene having a mass-average molecular weight of 5×105 or more and a heat of fusion of 90 J/g or more (measured by a differential scanning calorimeter). JP 2004-196871 A proposes a microporous polyolefin membrane comprising polyethylene, and polypropylene having a mass-average molecular weight of 5×105 or more and a melting point of 163° C. or higher (measured by a differential scanning calorimeter at a temperature-elevating speed of 3 to 20° C./minute) The microporous polyolefin membranes of JP 2004-196870 A and JP 2004-196871 A have shutdown temperatures of 120 to 140° C. and meltdown temperatures of 165° C. or higher, as well as excellent mechanical properties and permeability.
WO 97/23554 discloses a microporous membrane having high short-circuiting resistance (shutdown properties), which is made of high-density polyethylene or a linear ethylene copolymer having an end vinyl group concentration of 2 or more per 10,000 carbon atoms when measured by infrared spectroscopy, and a fuse temperature (shutdown temperature) of 131 to 136° C.
However, to improve the safety of lithium ion batteries, the microporous membranes are required to have not only low shutdown temperatures and high meltdown temperatures, but also improved air permeability change ratios (an index of shutdown speed) after the start of shutdown.
Accordingly, an object of this invention is to provide a microporous polyolefin membrane having a good balance of a high air permeability change ratio (an index of shutdown speed) after the start of shutdown, a low shutdown temperature, and meltdown properties, a battery separator formed thereby, and a battery.
Another object of this invention is to provide a microporous polyolefin membrane having a good balance of a low shutdown start temperature, a high air permeability change ratio after the start of shutdown, a low shutdown temperature, and meltdown properties, a battery separator formed thereby, and a battery.
As a result of intense research in view of the above objects, the inventors have found that a microporous polyolefin membrane having a good balance of a high air permeability change ratio after the start of shutdown, a low shutdown temperature and meltdown properties can be obtained by using a polyethylene resin having a temperature of 135° C. or lower, at which the crystal-melting calorie measured by differential scanning calorimetry at a predetermined temperature-elevating speed reaches 60% of the total crystal-melting calorie, a half-value of a melting endotherm curve (obtained by differential scanning calorimetry) of 10° C. or lower, and an angular frequency of 10 rad/sec or less, at which the storage modulus and the loss modulus obtained by melt viscoelasticity measurement are equal to each other at a predetermined temperature. The inventors also have found that a microporous polyolefin membrane having a good balance of a low shutdown start temperature, a high air permeability change ratio after the start of shutdown, a low shutdown temperature and meltdown properties can be obtained by using a polyethylene resin having a temperature of 125° C. or lower, at which the above crystal-melting calorie reaches 20% of the total crystal-melting calorie, a temperature of 135° C. or lower, at which the above crystal-melting calorie reaches 60% of the total crystal-melting calorie, and an angular frequency of 1 rad/sec or less, at which the storage modulus and the loss modulus are equal to each other. This invention has been completed based on such findings.
Thus, the first microporous polyolefin membrane of this invention is made of a polyethylene resin as a main component, and has (a) a shutdown temperature of 135° C. or lower, at which the air permeability measured while heating at a temperature-elevating speed of 5° C./minute reaches 1×105 sec/100 cm3, (b) an air permeability change ratio of 1×104 sec/100 cm3/° C. or more, which is a gradient of a curve representing the dependency of air permeability on a temperature at the air permeability of 1×104 sec/100 cm3, and (c) a meltdown temperature of 150° C. or higher, at which the air permeability measured while further heating after reaching the shutdown temperature becomes 1×105 sec/10) cm3 again.
In the first microporous polyolefin membrane, the polyethylene resin preferably has a temperature of 135° C. or lower, at which the crystal-melting calorie measured by differential scanning calorimetry at a constant temperature-elevating speed in a range of 3 to 20° C./minute reaches 60% of the total crystal-melting calorie; a half-value of a melting endotherm curve (obtained by differential scanning calorimetry) of 10° C. or lower, and an angular frequency of 10° C. or lower, and an angular frequency of 10 rad/sec or less, at which the storage modulus and the loss modulus obtained by melt viscoelasticity measurement at a constant temperature in a range of 160 to 220° C. are equal to each other.
The second microporous polyolefin membrane of this invention is made of a polyethylene resin as a main component, and has (a) a shutdown temperature of 135° C. or lower, at which the air permeability measured while heating at a temperature-elevating speed of 5° C./minute reaches 1×105 sec/100 cm3, (b) an air permeability change ratio of 1×104 sec/100 cm3/° C. or more, which is a gradient of a curve representing the dependency of air permeability on a temperature at the air permeability of 1×104 sec/100 cm3, (c) a shutdown start temperature of 130° C. or lower, which is determined from a curve representing the dependency of a reciprocal of the air permeability on a temperature, at an intersection of an extension of a straight portion of the curve after the start of temperature elevation and before the start of shutdown and an extension of a straight portion of the curve after the start of shutdown and before reaching the shutdown temperature, and (d) a meltdown temperature of 155° C. or higher, at which the air permeability measured while further heating after reaching the shutdown temperature becomes 1×105 sec/100 cm3 again.
In a preferred example of the second microporous polyolefin membrane, (e) the air permeability (converted to the value at 20-μm thickness) is 800 sec/100 cm3 or less, (f) the pin puncture strength (converted to the value at 20-μm thickness) is 4,000 mN or more, and (g) the heat shrinkage ratio measured after exposed to 105° C. for 8 hours is 8% or less.
In the second microporous polyolefin membrane, the polyethylene resin preferably has a temperature of 125° C. or lower, at which the crystal-melting calorie measured by differential scanning calorimetry at a constant temperature-elevating speed in a range of 3 to 20° C./minute reaches 20% of the total crystal-melting calorie, a temperature of 135° C. or lower, at which the crystal-melting calorie reaches 60% of the total crystal-melting calorie, and an angular frequency of 1 rad/sec or less, at which the storage modulus and the loss modulus obtained by melt viscoelasticity measurement at a constant temperature in a range of 160 to 220° C. are equal to each other.
The battery separator of this invention is formed by the first or second microporous polyolefin membrane.
The battery of this invention comprises a battery separator formed by the first or second microporous polyolefin membrane.
[1] First Polyolefin Resin
The first polyolefin resin forming the first microporous polyolefin membrane comprises the first polyethylene resin described below as a main component.
(1) Crystal-Melting Calorie and Dynamic Melt Viscoelasticity of First Polyethylene Resin
The first polyethylene resin has a temperature [hereinafter referred to as “T (60%)”] of 135° C. or lower, at which a crystal-melting calorie ΔHm measured by differential scanning calorimetry (DSC) at a constant temperature-elevating speed in a range of 3 to 20° C./minute reaches 60% of the total crystal-melting calorie, a half-value ΔTm of a melting endotherm curve (obtained by DSC) of 10° C. or lower, and an angular frequency ω0 of 10 rad/sec or less, at which the storage modulus (G′) and the loss modulus (G″) obtained by melt viscoelasticity measurement at a constant temperature in a range of 160 to 220° C. are equal to each other.
T (60%) is a parameter affected by the primary structure of polyethylene (homopolymer or ethylene-α-olefin copolymer), such as a molecular weight, a molecular weight distribution, a branching ratio, the molecular weight of branched chains, the distribution of branching points, the fractions of the copolymer, etc., and the high-order structure of polyethylene such as the size and distribution of crystals, crystal lattice regularity, etc., acting as an index of the shutdown temperature of the microporous polyolefin membrane. When T (60%) is higher than 135° C., the microporous polyolefin membrane exhibits a high shutdown temperature when used as a lithium battery separator.
The crystal-melting calorie ΔHm of the first polyethylene resin was measured by the following procedure according to JIS K7122. Namely, a sample of the first polyethylene resin (0.5-mm-thick molding melt-pressed at 210° C.) was placed in a sample holder of a differential scanning calorimeter (Pyris Diamond DSC available from Perkin Elmer, Inc.), heat-treated at 230° C. for 1 minute in a nitrogen atmosphere, cooled to 30° C. at 10° C./minute, kept at 30° C. for 1 minute, and heated to 230° C. at a speed of 3 to 20° C./minute. The temperature-elevating speed is preferably 5 to 15° C./minute, more preferably 10° C./minute. As shown in
ΔTm is a parameter affected by the size and distribution of crystals, crystal lattice regularity, etc. of the polyethylene, acting as an index of the shutdown speed. The larger ΔTm provides a longer time period from start to end of melting, resulting in a lower air permeability change ratio, an index of the shutdown speed, and slower overheat shutdown response when the microporous polyolefin membrane is used as a lithium battery separator. The ΔTm of 10° C. or lower provides a good shutdown speed. The ΔTm is preferably 9° C. or lower. The ΔTm (° C.) is a temperature difference between two points on the melting endotherm curve, at which a heat flux Q (Tm) is ½ of the heat flux at a peak Tm, as shown in
ω0 is a parameter affected by the characteristics of the polyethylene, such as a mass-average molecular weight (Mw), a molecular weight distribution and a branching ratio, and the molecular weight of branched chains, the distribution of branching points, the degree of entanglement of molecules, and a molecular weight between the entangling points of molecules, an index of the meltdown temperature. The ω0 of more than 10 rad/sec provides a lithium battery separator formed by the microporous polyolefin membrane with a low meltdown temperature, and poor rupture resistance during temperature elevation after shutdown, resulting in a low-stability battery. The ω0 is preferably 3 rad/sec or less. The lower limit of the ω0 is preferably 0.01 rad/sec. The ω0 of less than 0.01 rad/sec provides a high viscosity, and thus low extrudability. The ω0 of 0.01 to 1 rad/sec is particularly preferable.
The ω0 was measured under the following conditions using a commercially available melt viscoelasticity meter (RheoStress-300 available from Haake).
The response of G′ and G″ to an angular frequency ω was measured under the above conditions to depict a log ω-log G′ curve and a log ω-log G″ curve as shown in
(2) Composition of First Polyethylene Resin
The first polyethylene resin may be a single substance or a composition of two or more types of polyethylene, as long as its T (60%), ΔTm and ω0 are in the above ranges. The first polyethylene resin is preferably (a) ultra-high-molecular-weight polyethylene, (b) polyethylene other than the ultra-high-molecular-weight polyethylene, or (c) a mixture of the ultra-high-molecular-weight polyethylene and the other polyethylene (polyethylene composition). In any case, the mass-average molecular weight (Mw) of the first polyethylene resin is preferably 1×104 to 1×107, more preferably 5×104 to 15×106, particularly 1×105 to 5×106, though not particularly critical.
(a) Ultra-High-Molecular-Weight Polyethylene
The ultra-high-molecular-weight polyethylene has Mw of 7×105 or more. The ultra-high-molecular-weight polyethylene can be not only an ethylene homopolymer, but also an ethylene-α-olefin copolymer containing a small amount of another α-olefin. The other α-olefins than ethylene are preferably propylene, butene-1, pentene-1, hexene-1,4-methylpentene-1, octene-1, vinyl acetate, methyl methacrylate and styrene. The Mw of the ultra-high-molecular-weight polyethylene is preferably 1×106 to 15×106, more preferably 1×106 to 5×106.
(b) Polyethylene Other than Ultra-High-Molecular-Weight Polyethylene
The polyethylene other than the ultra-high-molecular-weight polyethylene has Mw of 1×104 or more and less than 7×105, being preferably high-density polyethylene, medium-density polyethylene, branched low-density polyethylene and linear low-density polyethylene, more preferably high-density polyethylene. The polyethylene having Mw of 1×104 or more and less than 7×105 can be not only an ethylene homopolymer, but also a copolymer containing a small amount of another α-olefin such as propylene, butene-1, hexene-1, etc. Such copolymers are preferably produced using single-site catalysts. The polyethylene other than the ultra-high-molecular-weight polyethylene can be not only a single substance, but also a mixture of two or more polyethylenes other than the ultra-high-molecular-weight polyethylene.
(c) Polyethylene Composition
The polyolefin composition is a mixture of the ultra-high-molecular-weight polyethylene having Mw of 7×105 or more with the other polyethylene having Mw of 1×104 or more and less than 7×105 (at least one selected from the group consisting of high-density polyethylene, medium-density polyethylene, branched low-density polyethylene, and linear low-density polyethylene). The ultra-high-molecular-weight polyethylene and the other polyethylene can be the same as described above. The molecular weight distribution [mass-average molecular weight/number-average molecular weight (Mw/Mn)] of this polyethylene composition can easily be controlled depending on applications. The preferred polyethylene composition comprises the above ultra-high-molecular-weight polyethylene and high-density polyethylene. The high-density polyethylene used in the polyethylene composition has Mw of preferably 1×105 to 7×105, more preferably 1×105 to 5×105, most preferably 2.6×105 to 4×105. The amount of the ultra-high-molecular-weight polyethylene in the polyethylene composition is preferably 1% by mass or more, more preferably 2 to 50% by mass, based on 100% by mass of the entire polyethylene composition.
(d) Molecular Weight Distribution Mw/Mn
Mw/Mn is a measure of the molecular weight distribution, and the larger this value is, the wider the molecular weight distribution is. The Mw/Mn of the first polyethylene resin is preferably 5 to 300, more preferably 10 to 100, though not critical, when the polyethylene resin is the ultra-high-molecular-weight polyethylene, the polyethylene other than the ultra-high-molecular-weight polyethylene, or the polyethylene composition. When the Mw/Mn is less than 5, there are excessive high-molecular weight components, resulting in difficulty in melt extrusion. When the Mw/Mn is more than 300, there are excessive low-molecular weight components, resulting in a microporous membrane with decreased strength. The Mw/Mn of polyethylene (homopolymer or ethylene-α-olefin copolymer) can properly be controlled by multi-stage polymerization. The multi-stage polymerization method is preferably a two-stage polymerization method comprising forming a high-molecular-weight polymer component in the first stage and forming a low-molecular-weight polymer component in the second stage. In the case of the polyethylene composition, the larger the Mw/Mn, the larger difference in Mw between the ultra-high-molecular-weight polyethylene and the other polyethylene, and vice versa. The Mw/Mn of the polyethylene composition can be properly controlled by the molecular weight and percentage of each component.
Such first polyethylene resins are commercially available, for instance, as Nipolon Hard 6100A, 7300A and 5110A, 6510A, 6530A and 6200A from Tosoh Corporation, and HI-ZEX 640UF and 780UF from Prime Polymer Co., Ltd.
(3) Addable Other Resins
The first polyolefin resin may contain a polyolefin other than polyethylene or a resin other than the polyolefin in a range not deteriorating the effect of this invention. Accordingly, it should be noted that the term “polyolefin resin” includes not only a polyolefin but also a resin other than the polyolefin. The polyolefin other than polyethylene can be at least one selected from the group consisting of polypropylene, polybutene-1, polypentene-1, polyhexene-1, poly-4-methylpentene-1, polyoctene-1, polyvinyl acetate, polymethyl methacrylate, polystyrene and ethylene-α-olefin copolymers each having Mw of 1×104 to 4×106, and a polyethylene wax having Mw of 1×103 to 1×104. Polypropylene, polybutene-1, polypentene-1, polyhexene-1, poly-4-methylpentene-1, polyoctene-1, polyvinyl acetate, polymethyl methacrylate and polystyrene may be homopolymers or copolymers containing other α-olefins.
The resin other than the polyolefin includes a heat-resistant resin having a melting point or glass transition temperature (Tg) of 150° C. or higher. The heat-resistant resin is preferably a crystalline resin (including partially crystalline resin) having a melting point of 150° C. or higher, or an amorphous resin having Tg of 150° C. or higher. The melting point and Tg can be measured according to JIS K7121.
Because a battery separator formed by a microporous polyolefin membrane comprising the first polyethylene resin containing the heat-resistant resin has an improved meltdown temperature, batteries are provided with improved high-temperature storage stability. Though not particularly critical, the upper limit of the melting point or Tg of the heat-resistant resin is preferably 350° C. or lower from the aspect of easy blending with the first polyethylene resin. The melting point or Tg of the heat-resistant resin is more preferably 170 to 260° C.
Specific examples of the heat-resistant resin include polyesters such as polybutylene terephthalate (melting point: about 160 to 230° C.) and polyethylene terephthalate (melting point: about 250 to 270° C.), fluororesins, polyamides (melting point: 215 to 265° C.), polyarylene sulfides, isotactic polystyrene (melting point: 230° C.), polyimides (Tg: 280° C. or higher), polyamideimides (Tg: 280° C.), polyethersulfone (Tg: 223° C.), polyetheretherketone (melting point: 334° C.), polycarbonates (melting point: 220 to 240° C.), cellulose acetate (melting point: 220° C.), cellulose triacetate (melting point: 300° C.), polysulfone (Tg: 190° C.), polyetherimides (melting point: 216° C.), etc. The heat-resistant resin can be composed of a single resin component or pluralities of resin components.
The heat-resistant resin content is preferably 3 to 30% by mass, more preferably 5 to 25% by mass, based on 100% by mass of the total amount of the first polyethylene resin and the heat-resistant resin When this content is more than 30% by mass, the membrane has low pin puncture strength, tensile rupture strength and flatness.
[2] Second Polyolefin Resin
The second polyolefin resin forming the second microporous polyolefin membrane comprises the second polyethylene resin described below as a main component.
(1) Crystal-Melting Calorie and Dynamic Melt Viscoelasticity of Second Polyethylene Resin
The second polyethylene resin has a temperature [hereinafter referred to as “T (20%)”] of 125° C. or lower, at which a crystal-melting calorie ΔHm measured by differential scanning calorimetry (DSC) at a constant temperature-elevating speed in a range of 3 to 20° C./minute reaches 20% of the total crystal-melting calorie, T (60%) of 135° C. or lower, and ω0 of 1 rad/sec or less.
T (20%) is also a parameter affected by the primary structure of polyethylene (homopolymer or ethylene-α-olefin copolymer) such as a molecular weight, a molecular weight distribution, a branching ratio, the molecular weight of branched chains, the distribution of branching points, the percentage of copolymers, etc., and the high-order structure of the polyethylene such as the size and distribution of crystals, crystal lattice regularity, etc. In the second polyethylene resin, T (20%) and T (60%) are indexes of the shutdown start temperature and the shutdown temperature. When T (20%) is higher than 125° C., or when T (60%) is higher than 135° C., a lithium battery separator formed by the microporous polyolefin membrane has high shutdown start temperature or shutdown temperature, and low shutdown response when overheated.
As described above, an area S1 of a region enclosed by a DSC curve (melting endotherm curve) obtained in the course of temperature elevation according to JIS K7122 and the baseline was determined (see
Like above, ω0 is an index of the meltdown temperature. The ω0 of 1 rad/sec or less provides excellent meltdown properties. In the second polyethylene resin, the ω0 is preferably 0.8 rad/sec or less, more preferably 0.1 rad/sec or less. The lower limit of the ω0 is preferably 0.01 rad/sec. The ω0 was determined by the same method as described above.
(2) Composition of Second Polyethylene Resin
The second polyethylene resin may be a single substance or a composition of two or more types of polyethylene, as long as its T (20%), T (60%) and ω0 are within the above ranges. The second polyethylene resin is also preferably (a) ultra-high-molecular-weight polyethylene, (b) polyethylene other than the ultra-high-molecular-weight polyethylene, or (c) a mixture of the ultra-high-molecular-weight polyethylene and the other polyethylene (polyethylene composition). The ultra-high-molecular-weight polyethylene, the polyethylene other than the ultra-high-molecular-weight polyethylene, and the polyethylene composition may be the same as above.
Such second polyethylene resins are commercially available, for instance, as GUR from Ticona Japan Ltd., Novatec HF311 from Japan Polyethylene Co., Ltd., Nipolon Hard 6100A, 7300A and 5100A from Tosoh Corporation, HI-ZEX 640UF and 780UF from Prime Polymer Co., Ltd.
The second polyolefin resin may also contain a polyolefin other than the polyethylene and the above heat-resistant resin in a range not deteriorating the effect of this invention. these percentages may also be the same as above.
[3] Inorganic Fillers
Inorganic fillers may be added to the first or second polyolefin resin. The inorganic fillers include silica, alumina, silica-alumina, zeolite, mica, clay, kaolin, talc, calcium carbonate, calcium oxide, calcium sulfate, barium carbonate, barium sulfate, magnesium carbonate, magnesium sulfate, magnesium oxide, diatomaceous earth, glass powder, aluminum hydroxide, titanium dioxide, zinc oxide, satin white, acid clay, etc. The inorganic fillers can be used alone or in combination. Among them, silica or calcium carbonate is preferably used. The amount of inorganic fillers added is preferably 0.1 to 5 parts by mass, more preferably 0.5 to 3 parts by mass, based on 100 parts by mass of the total amount of the polyolefin resin and the fillers.
[4] Production Method of First Microporous Polyolefin Membrane
The production method of the first microporous polyolefin membrane comprises the steps of (1) melt-blending the first polyolefin resin and a membrane-forming solvent to prepare a polyolefin resin solution, (2) extruding the polyolefin resin solution through a die, (3) cooling the resultant extrudate to form a gel-like sheet, (4) removing the membrane-forming solvent, and (5) drying the membrane. Namely, the first microporous polyolefin membrane is produced by a so-called wet method. Before the step (4), if necessary, a stretching step (6), a heat roll treatment step (7), a hot solvent treatment step (8) and a heat-setting step (9) can be conducted. After the step (5), a step (10) of stretching a microporous membrane, a heat treatment step (11), a cross-linking step (12) with ionizing radiations, a hydrophilizing step (13), a surface-coating step (14), etc. can be conducted. Incidentally, a dry method in which pores are formed by stretching may be advantageous than the wet method in a shutdown temperature, a shutdown speed, etc.
(1) Preparation of Polyolefin Resin Solution
The first polyolefin resin and a proper membrane-forming solvent are melt-blended to prepare a polyolefin resin solution. The polyolefin resin solution can contain various additives such as the above fillers, antioxidants, ultraviolet absorbents, antiblocking agents, pigments, dyes, etc., if necessary, in ranges not deteriorating the effects of this invention. Fine silicate powder, for instance, can be added as a pore-forming agent.
The membrane-forming solvent can be liquid or solid. The liquid solvents can be aliphatic or cyclic hydrocarbons such as nonane, decane, decalin, p-xylene, undecane, dodecane, liquid paraffin, etc.; and mineral oil distillates having boiling points corresponding to those of the above hydrocarbons. To obtain a gel-like sheet having a stable liquid solvent content, non-volatile liquid solvents such as liquid paraffin are preferable. The solid solvent preferably has melting point of 80° C. or lower. Such solid solvents are paraffin wax, ceryl alcohol, stearyl alcohol, dicyclohexyl phthalate, etc. The liquid solvent and the solid solvent can be used in combination.
The viscosity of the liquid solvent is preferably 30 to 500 cSt, more preferably 30 to 200 cSt, at 25° C. When the viscosity at 25° C. is less than 30 cSt, the solution is easily foamed, resulting in difficulty in blending. The viscosity of more than 500 cSt makes the removal of the liquid solvent difficult.
Though not particularly critical, the uniform melt blending of the polyolefin resin solution is preferably conducted in a double-screw extruder. Melt blending in the double-screw extruder is suitable for preparing a high-concentration polyolefin resin solution. The melt-blending temperature of the polyolefin resin solution is preferably in a range from the melting point Tm1 of the first polyolefin resin+10° C. to the melting point Tm1+100° C. The melting point Tm1 of the first polyolefin resin is the melting point of (a) the ultra-high-molecular-weight polyethylene, (b) the polyethylene other than the ultra-high-molecular-weight polyethylene, or (c) the polyethylene composition, when the first polyolefin resin is any one of them. When the first polyolefin resin is the composition containing the polyolefin other than the polyethylene or the heat-resistant resin, the melting point Tm1 of the first polyolefin resin is the melting point of ultra-high-molecular-weight polyethylene, the other polyethylene, or the polyethylene composition, which is contained in the above composition. The ultra-high-molecular-weight polyethylene, the polyethylene other than the ultra-high-molecular-weight polyethylene and the polyethylene composition have melting points of about 130 to 140° C. Accordingly, the melt-blending temperature is preferably 140 to 250° C., more preferably 170 to 240° C.
When the first polyolefin resin contains the heat-resistant resin, the melt-blending temperature is preferably in a range from the melting point of the heat-resistant resin to the melting point+100° C., more preferably in a range from the melting point of the heat-resistant resin to the melting point Tm1+100° C. The membrane-forming solvent may be added before the start of blending or introduced into the double-screw extruder at an intermediate point during blending, through the latter is preferable. In the melt blending, the antioxidant is preferably added to prevent the oxidation of the first polyolefin resin.
The concentration of the first polyolefin resin is 10 to 50% by mass, preferably 20 to 45% by mass, based on 100% by mass of the total amount of the first polyolefin resin and the membrane-forming solvent. Less than 10% by mass of the first polyolefin resin undesirably lowers productivity. In addition, large swelling and neck-in occur at the die exit in the extrusion of the polyolefin resin solution, resulting in decrease in the formability and self-supportability of the extrudate. More than 50% by mass of the first polyolefin resin lowers the formability of the extrudate.
(2) Extrusion
The melt-blended polyolefin resin solution is extruded through a die directly or indirectly from the extruder. Alternatively, it may be cooled to pellets, introduced into the extruder again, and then extruded through the die. Although a sheet-forming die having a rectangular orifice is usually used, a double-cylindrical, hollow die, an inflation die lip, etc. can also be used. The sheet-forming die usually has a die gap of 0.1 to 5 mm, and is heated at 140 to 250° C. during extrusion. The extrusion speed of the heated solution is preferably 0.2 to 15 m/minute.
(3) Formation of Gel-Like Sheet
An extrudate exiting from the die is cooled to provide a gel-like sheet. The cooling is preferably conducted to at least a gelation temperature at a speed of 50° C./minute or more. Such cooling fixes microphase separation between the first polyolefin resin and the membrane-forming solvent, thereby providing a fixed gel structure comprising a first polyolefin resin phase and a membrane-forming solvent phase. The cooling is preferably conducted to 25° C. or lower. In general, a low cooling speed provides the gel-like sheet with a coarse high-order structure having large pseudo-cell units, while a high cooling speed provides dense cell units. The cooling speed of less than 50° C./minute increases crystallization, making it difficult to form a stretchable gel-like sheet. The cooling method can be a method of bringing the extrudate into contact with a cooling medium such as cooling air, cooling water, etc., a method of bring the extrudate into contact with a cooling roll, etc., and the cooling method using a cooling roll is preferable.
The temperature of the cooling roll is preferably (the crystallization temperature Tc1 of the first polyolefin resin—115° C.) to Tc1, more preferably (Tc1−110° C.) to (Tc1—10° C.). When the temperature of the cooling roll is higher than Tc1, sufficiently rapid cooling cannot be conducted. The crystallization temperature Tc1 of the first polyolefin resin is the crystallization temperature of (a) the ultra-high-molecular-weight polyethylene, (b) the polyethylene other than the ultra-high-molecular-weight polyethylene, or (c) the polyethylene composition, when the first polyolefin resin is any one of them. When the first polyolefin resin is a composition containing the polyolefin other than the polyethylene or the heat-resistant resin, it is the crystallization temperature of the ultra-high-molecular-weight polyethylene, the other polyethylene or the polyethylene composition, which is contained in the above composition. The crystallization temperature is measured according to JIS K7121. The ultra-high-molecular-weight polyethylene, the other polyethylene and the polyethylene composition generally have crystallization temperatures of 102 to 108° C. Accordingly, the temperature of the cooling roll is in a range from −10° C. to 105° C., preferably in a range from −5° C. to 95° C. The contact time of the cooling roll with the sheet is preferably 1 to 30 seconds, more preferably 2 to 15 seconds.
(4) Removal of Membrane-Forming Solvent
The liquid solvent is removed (washed away) using a washing solvent. Because the first polyolefin resin phase is separated from the membrane-forming solvent phase in the gel-like sheet, the removal of the liquid solvent provides a microporous membrane. The removal (washing away) of the liquid solvent can be conducted by using a known washing solvent. The washing solvents can be volatile solvents, for instance, saturated hydrocarbons such as pentane, hexane, heptane, etc.; chlorinated hydrocarbons such as methylene chloride, carbon tetrachloride, etc.; ethers such as diethyl ether, dioxane, etc.; ketones such as methyl ethyl ketone, etc.; linear fluorocarbons such as trifluoroethane, C6F14, C7F16, etc.; cyclic hydrofluorocarbons such as C5H3F7, etc.; hydrofluoroethers such as C4F9OCH3, C4F9OC2H5, etc.; and perfluoroethers such as C4F9OCF3, C4F9OC2F5, etc. These washing solvents have a low surface tension, for instance, 24 mN/m or less at 25° C. The use of a washing solvent having a low surface tension suppresses a pore-forming network structure from shrinking due to a surface tension of gas-liquid interfaces during drying after washing, thereby providing a microporous membrane having high porosity and permeability.
The washing of the membrane can be conducted by a washing-solvent-immersing method, a washing-solvent-showering method, or a combination thereof. The amount of the washing solvent used is preferably 300 to 30,000 parts by mass, per 100 parts by mass of the membrane before washing. Washing with the washing solvent is preferably conducted until the amount of the remaining liquid solvent becomes less than 1% by mass of that added.
(5) Drying of Membrane
The microporous polyolefin membrane obtained by removing the membrane-forming solvent is then dried by a heat-drying method, a wind-drying method, etc. The drying temperature is preferably equal to or lower than the crystal dispersion temperature Tcd1 of the first polyolefin resin, particularly lower than the Tcd1 by 5° C. or more.
The crystal dispersion temperature Tcd1 of the first polyolefin resin is the crystal dispersion temperature of (a) the ultra-high-molecular-weight polyethylene, (b) the polyethylene other than the ultra-high-molecular-weight polyethylene, or (c) the polyethylene composition, when the first polyolefin resin is any one of them. When the first polyolefin resin is a composition containing the polyolefin other than polyethylene or the heat-resistant resin, it is the crystal dispersion temperature of the ultra-high-molecular-weight polyethylene, the other polyethylene or the polyethylene composition, which is contained in the above composition. The crystal dispersion temperature is determined by the measurement of the temperature characteristics of dynamic viscoelasticity according to ASTM D 4065. The ultra-high-molecular-weight polyethylene, the polyethylene other than the ultra-high-molecular-weight polyethylene and the polyethylene composition have crystal dispersion temperatures of about 90 to 100° C.
Drying is conducted until the percentage of the remaining washing solvent becomes preferably 5% or less by mass, more preferably 3% or less by mass, based on 100% by mass of the microporous membrane (dry weight). Insufficient drying undesirably reduces the porosity of the microporous membrane when heat-treated subsequently, thereby resulting in poor permeability.
(6) Stretching
The gel-like sheet before washing is preferably stretched at least monoaxially. After heating, the gel-like sheet is preferably stretched to a predetermined magnification by a tenter method, a roll method, an inflation method, a rolling method, or their combination. Because the gel-like sheet contains a membrane-forming solvent, it can be uniformly stretched. The stretching is particularly preferable when used for battery separators, because it improves the mechanical strength and expands pores. Although the stretching can be monoaxial or biaxial, biaxial stretching is preferable. The biaxial stretching can be simultaneous biaxial stretching, sequential stretching, or multi-stage stretching (for instance, a combination of simultaneous biaxial stretching and sequential stretching), though the simultaneous biaxial stretching is particularly preferable.
The stretching magnification is preferably 2-fold or more, more preferably 3- to 30-fold in the case of monoaxial stretching. In the case of biaxial stretching, it is at least 3-fold in both directions, preferably with an area magnification of 9-fold or more, The area magnification of less than 9-fold results in insufficient stretching, failing to providing a high-modulus, high-strength microporous membrane. When the area magnification is more than 400-fold, restrictions occur on stretching apparatuses, stretching operations, etc. The upper limit of the area magnification is preferably 50-fold.
The stretching temperature is preferably equal to or lower than the melting point Tm1 of the first polyolefin resin+10° C., more preferably in a range of the crystal dispersion temperature Tcd1 or higher and lower than the melting point Tm1+10° C. When this stretching temperature exceeds the melting point Tm+10° C., the first polyethylene resin is molten, so that stretching fails to orient molecular chains. When it is lower than the crystal dispersion temperature Tcd1, the first polyethylene resin is insufficiently softened, making it likely that the membrane is broken by stretching, thus failing to achieve high-magnification stretching. As described above, the first polyethylene resin has a crystal dispersion temperature of about 90 to 100° C. Accordingly, the stretching temperature is usually in a range of 90 to 140° C., preferably in a range of 100 to 130° C.
The above stretching causes cleavage between polyethylene crystal lamellas, making the polyethylene phase (the ultra-high-molecular-weight polyethylene, the other polyethylene or the polyethylene composition) finer with larger numbers of fibrils. The fibrils form a three-dimensional network structure (three-dimensionally and irregularly connected network structure).
Depending on the desired properties, stretching can be conducted with a temperature distribution in a thickness direction, to provide a microporous membrane with higher mechanical strength. This method is described specifically in Japanese Patent 3347854.
(7) Hot Roll Treatment
At least one surface of the gel-like sheet can be brought into contact with a heat roll. This method is specifically described, for instance, in Japanese Patent application 2005-271046.
(8) Hot Solvent Treatment
The gel-like sheet can be treated with a hot solvent. This method is specifically described in WO 2000/20493.
(9) Heat Setting
The stretched gel-like sheet is preferably heat-set. This method is specifically described, for instance, in JP 2002-256099 A.
(10) Stretching of Microporous Membrane
The dried microporous polyolefin membrane can be stretched at least monoaxially in a range not deteriorating the effect of this invention. This stretching can be conducted by a tenter method, etc. while heating the membrane, in the same manner as described above.
The temperature of stretching the microporous membrane is preferably equal to or lower than the melting point Tm1 of the first polyolefin resin, more preferably in a range from the crystal dispersion temperature Tcd1 to the melting point Tm1. Specifically, it is in a range of 90 to 135° C., preferably in a range of 95 to 130° C. In the case of biaxial stretching, it is preferably 1.1- to 2.5-fold, more preferably 1.1- to 2.0-fold, at least monoaxially. When this magnification is more than 2.5-fold, the shutdown temperature may be deteriorated.
(11) Heat Treatment
The dried membrane is preferably heat-set and/or annealed by known methods. They may be properly selected depending on properties required on the microporous polyolefin membrane.
(12) Cross-Linking of Membrane
The dried microporous polyolefin membrane can be cross-linked by ionizing radiation of α-rays, β-rays, γ-rays, electron beams, etc. The electron beam irradiation is preferably conducted at 0.1 to 100 Mrad and accelerating voltage of 100 to 300 kV. The cross-linking treatment elevates the meltdown temperature of the microporous membrane.
(13) Hydrophilizing
The dried microporous polyolefin membrane can be hydrophilized by a monomer-grafting treatment, a surfactant treatment, a corona-discharging treatment, a plasma treatment, etc., which are known.
(14) Surface Coating
The dried microporous polyolefin membrane can be coated with a porous fluororesin such as polyvinylidene fluoride and polytetrafluoroethylene, porous polyimide, porous polyphenylene sulfide, etc., to improve meltdown properties when used as a battery separator. A coating layer comprising polypropylene may be formed on at least one surface of the dried microporous polyolefin membrane. The containing polypropylene is described, for instance, in WO2005-054350.
[5] Production Method of Second Microporous Polyolefin Membrane
The production method of the second microporous polyolefin membrane may be the same as the production method of the first microporous polyolefin membrane except for using the second polyolefin resin in place of the first polyolefin resin. While the melt-blending temperature, the cooling temperature of an extrudate, the drying temperature, the stretching temperature of a gel-like sheet and the stretching temperature of a microporous membrane are determined depending on the crystallization temperature Tc1, crystal dispersion temperature Tcd1 or melting point Tm1 of the first polyolefin resin in the production method of the first microporous polyolefin membrane, these temperatures are determined depending on the crystallization temperature Tc2, crystal dispersion temperature Tcd2 or melting point Tm2 of the second polyolefin resin in the production method of the second microporous polyolefin membrane.
The crystallization temperature Tc2 of the second polyolefin resin is the crystallization temperature of (a) the ultra-high-molecular-weight polyethylene, (b) the polyethylene other than the ultra-high-molecular-weight polyethylene, or (c) the polyethylene composition, when the second polyolefin resin is any one of them. When the second polyolefin resin is a composition comprising the polyolefin other than polyethylene or the heat-resistant resin, it is the crystallization temperature of the ultra-high-molecular-weight polyethylene, the other polyethylene or the polyethylene composition, which is contained in the above composition.
The crystal dispersion temperature Tcd2 of the second polyolefin resin is the crystal dispersion temperature of (a) the ultra-high-molecular-weight polyethylene, (b) the polyethylene other than the ultra-high-molecular-weight polyethylene, or (c) the polyethylene composition, when the second polyolefin resin is any one of them. When the second polyolefin resin is a composition comprising the polyolefin other than polyethylene or the heat-resistant resin, it is the crystal dispersion temperature of the ultra-high-molecular-weight polyethylene, the other polyethylene or the polyethylene composition, which is contained in the above composition.
The melting point Tm2 of the second polyolefin resin is the melting point of (a) the ultra-high-molecular-weight polyethylene, (b) the polyethylene other than the ultra-high-molecular-weight polyethylene, or (c) the polyethylene composition, when the second polyolefin resin is any one of them. When the second polyolefin resin is a composition comprising the polyolefin other than polyethylene or the heat-resistant resin, it is the melting point of the ultra-high-molecular-weight polyethylene, the other polyethylene or the polyethylene composition, which is contained in the above composition.
[6] Properties of First Microporous Polyolefin Membrane
The first microporous polyolefin membrane has the following properties.
(1) Shutdown temperature of 135° C. or lower
When the shutdown temperature is higher than 135° C., a lithium battery separator formed by the microporous polyolefin membrane has low shutdown response when overheated.
(2) Air permeability change ratio of 1×104 sec/100 cm3/° C. or more
The air permeability change ratio after the start of shutdown is 1×104 sec/100 cm3/° C. or more. When the air permeability change ratio is less than 1×104 sec/100 cm3/° C., a lithium battery separator formed by the microporous polyolefin membrane has low shutdown response when overheated.
(3) Meltdown temperature of 150° C. or higher
When the meltdown temperature is lower than 150° C., the microporous membrane has poor rupture resistance during temperature elevation after shutdown.
The first microporous polyolefin membrane according to a preferred embodiment of this invention also has the following properties.
(4) Air permeability of 20 to 800 sec/100 cm3 (converted to the value at 20-μm thickness)
When the air permeability is 20 to 800 sec/100 cm3 (converted to the value at 20-μm thickness), a separator formed by microporous polyolefin membrane provides a battery with large capacity and good cycle characteristics. When the air permeability is less than 20 sec/100 cm3, shutdown does not occur sufficiently when the temperature elevates in the battery.
(5) Porosity of 25 to 80%
With the porosity of less than 25%, the microporous polyolefin membrane does not have good air permeability. When the porosity exceeds 80%, the microporous polyolefin membrane used as a battery separator does not have enough strength, resulting in a high likelihood of short-circuiting between electrodes.
(6) Pin puncture strength of 3,000 mN/20 μm or more
With the pin puncture strength of less than 3,000 mN/20 μm, a battery comprising the microporous polyolefin membrane as a separator likely suffers short-circuiting between electrodes. The pin puncture strength is preferably 3,500 mN/20 μm or more.
(7) Tensile rupture strength of 80,000 kPa or more
With the tensile rupture strength of 80,000 kPa or more in both longitudinal direction (MD) and transverse direction (TD), the microporous membrane is unlikely ruptured when used as a battery separator. The tensile rupture strength is preferably 100,000 kPa or more in both MD and TD.
(8) Tensile rupture elongation of 80% or more
With the tensile rupture elongation of 80% or more in both longitudinal direction (MD) and transverse direction (TD), the microporous membrane is unlikely ruptured when used as a battery separator.
(9) Heat shrinkage ratio of 10% or less
The heat shrinkage ratio measured after exposed at 105° C. for 8 hours is 10% or less in both longitudinal direction (MD) and transverse direction (TD) after exposed to 105° C. for 8 hours. When the heat shrinkage ratio exceeds 10%, a battery separator formed by the microporous polyolefin membrane shrinks by heat generated therein, making it highly likely that short-circuiting occurs in the end portions of the separator. The heat shrinkage ratio is preferably 8% or less in both MD and TD.
Thus, the first microporous polyolefin membrane has a high air permeability change ratio after the start of shutdown, a low shutdown temperature, and a high meltdown temperature, as well as excellent permeability, mechanical properties and heat shrinkage resistance.
[7] Properties of Second Microporous Polyolefin Membrane
The second microporous polyolefin membrane has the following properties.
(1) Shutdown temperature of 135° C. or lower
(2) Air permeability change ratio of 1×104 sec/100 cm3/° C. or more
(3) Shutdown start temperature of 130° C. or lower
When the shutdown start temperature is 130° C. or lower, a lithium battery separator formed by the microporous polyolefin membrane has high shutdown response when overheated.
(4) Meltdown temperature of 155° C. or higher
The second microporous polyolefin membrane according to a preferred embodiment of this invention has pin puncture strength, air permeability, porosity, tensile rupture strength, tensile rupture elongation and heat shrinkage ratio, which are in the same ranges as those of the first microporous polyolefin membrane. However, the pin puncture strength is preferably 4,000 mN or more, more preferably 4,500 mN/20 μm or more.
Thus, the second microporous polyolefin membrane has a low shutdown start temperature, a high air permeability change ratio after the start of shutdown, a low shutdown temperature, and a high meltdown temperature, as well as excellent permeability, mechanical properties and heat shrinkage resistance.
[8] Battery Separator
The thickness of the battery separator formed by the first or second microporous polyolefin membrane is preferably 5 to 50 μm, more preferably 7 to 35 μm, though properly selectable depending on the types of batteries.
[9] Battery
The first and second microporous polyolefin membranes can be used preferably as separators for secondary batteries such as nickel-hydrogen batteries, nickel-cadmium batteries, nickel-zinc batteries, silver-zinc batteries, lithium secondary batteries, lithium polymer secondary batteries, etc., particularly as separators for lithium secondary batteries. Taking the lithium secondary battery for example, description will be made below.
The lithium secondary battery comprises a cathode and an anode laminated via a separator, the separator containing an electrolytic solution (electrolyte). The electrode can be of any known structure, not particularly critical. The electrode structure can be, for instance, a coin type in which disc-shaped cathode and anode are opposing, a laminate type in which planar cathode and anode are alternately laminated, a toroidal type in which ribbon-shaped cathode and anode are wound, etc.
The cathode usually comprises (a) a current collector, and (b) a cathodic active material layer capable of absorbing and discharging lithium ions, which is formed on the current collector. The cathodic active materials can be inorganic compounds such as transition metal oxides, composite oxides of lithium and transition metals (lithium composite oxides), transition metal sulfides, etc. The transition metals can be V, Mn, Fe, Co, Ni, etc. Preferred examples of the lithium composite oxides are lithium nickelate, lithium cobaltate, lithium manganate, laminar lithium composite oxides having an α-NaFeO2 structure, etc. The anode comprises (a) a current collector, and (b) an anodic active material layer formed on the current collector. The anodic active materials can be carbonaceous materials such as natural graphite, artificial graphite, cokes, carbon black, etc.
The electrolytic solutions can be obtained by dissolving lithium salts in organic solvents. The lithium salts can be LiClO4, LiPF6, LiAsF6, LiSbF6, LiBF4, LiCF3SO3, LiN(CF3SO2)2, LiC(CF3SO2)3, Li2B10Cl10, LiN(C2F5SO2)2, LiPF4(CF3)2, LiPF3(C2F5)3, lower aliphatic carboxylates of lithium, LiAlCl4, etc. The lithium salts can be used alone or in combination. The organic solvents can be organic solvents having high boiling points and high dielectric constants, such as ethylene carbonate, propylene carbonate, ethylmethyl carbonate, γ-butyrolactone, etc.; organic solvents having low boiling points and low viscosity, such as tetrahydrofuran, 2-methyltetrahydrofuran, dimethoxyethane, dioxolane, dimethyl carbonate, diethyl carbonate, etc. These organic solvents can be used alone or in combination. Because organic solvents having high dielectric constants have high viscosity, while those having low viscosity have low dielectric constants, their mixtures are preferably used.
When the battery is assembled, the separator can be impregnated with the electrolytic solution, so that the separator (microporous polyolefin membrane) is provided with ion permeability. The impregnation treatment is usually conducted by immersing the microporous polyolefin membrane in the electrolytic solution at room temperature. When a cylindrical battery is assembled, for instance, a cathode sheet, a separator formed by the microporous polyolefin membrane, and an anode sheet are laminated in this order, and the resultant laminate is wound to a toroidal-type electrode assembly. The resulting electrode assembly can be charged into a battery can and impregnated with the above electrolytic solution. A battery lid acting as a cathode terminal equipped with a safety valve can be caulked to the battery can via a gasket to produce a battery.
This invention will be described in more detail with reference to Examples below without intention of restricting the scope of this invention.
100 parts by mass of a polyethylene (PE) composition comprising 30% by mass of ultra-high-molecular-weight polyethylene (UHMWPE) having a mass-average molecular weight (Mw) of 2.5×106 and 70% by mass of high-density polyethylene (HDPE) having Mw of 2.8×105 was dry-blended with 0.375 parts by mass of tetrakis[methylene-3-(3,5-ditertiary-butyl-4-hydroxyphenyl)-propionate] methane. Measurement revealed that the PE composition comprising UHMWPE and HDPE had T (60%) of 134.3° C., ΔTm of 7.9° C., and ω0 of 0.55 rad/sec (measured at 180° C.).
The Mws of UHMWPE and HDPE were measured by a gel permeation chromatography (GPC) method under the flowing conditions (the same conditions applied below).
30 parts by mass of the resultant mixture was charged into a strong-blending, double-screw extruder (inner diameter=58 mm, L/D=42), and 70 parts by mass of liquid paraffin was supplied to the double-screw extruder via its side feeder. Melt blending was conducted at 210° C. and 200 rpm to prepare a polyethylene solution.
The polyethylene solution was supplied from the double-screw extruder to a T-die, and extruded in a 1.0-mm-thick sheet shape. The extrudate was cooled by a cooling roll controlled at 50° C. to form a gel-like sheet. The gel-like sheet was simultaneously biaxially stretched by a batch-type stretching machine to 5-fold in both longitudinal direction (MD) and transverse direction (TD) at 115° C. Fixed to an aluminum frame plate of 20 cm×20 cm, the stretched gel-like sheet was immersed in a washing bath of methylene chloride controlled at 25° C., and washed while swaying at 100 rpm for 3 minutes to remove the liquid paraffin. The washed membrane was air-dried at room temperature. Fixed to a tenter, the dried membrane was heat-set at 125° C. for 10 minutes to produce a microporous polyethylene membrane.
A microporous polyethylene membrane was produced in the same manner as in Example 1 except for using a polyethylene composition comprising 20% by mass of UHMWPE and 80% by mass of HDPE, which had T (60%) of 133.9° C., ΔTm of 7.1° C., and ω0 of 0.73 rad/sec.
A microporous polyethylene membrane was produced in the same manner as in Example 1 except for using a polyethylene composition comprising 20% by mass of UHMWPE having Mw of 2.0×106 and 80% by mass of HDPE, which had T (60%) of 134° C., ΔTm of 7.3° C., and ω0 of 0.82 rad/sec.
A microporous polyethylene membrane was produced in the same manner as in Example 1 except for using a polyethylene composition comprising 20% by mass of UHMWPE and 80% by mass of HDPE having Mw of 3.0×106, which had T (60%) of 134.4° C., ΔTm of 8.1° C., and ω0 of 0.025 rad/sec.
A microporous polyethylene membrane was produced in the same manner as in Example 1 except for using a polyethylene composition comprising 30% by mass of UHMWPE having Mw of 2.2×106 and 70% by mass of HDPE having Mw of 2.5×105, which had T (60%) of 135.7° C., ΔTm of 12.5° C., and ω0 of 2.4 rad/sec.
A microporous polyethylene membrane was produced in the same manner as in Example 1 except for using only HDPE having Mw of 2.5×105, T (60%) of 135.3° C., ΔTm of 10.3° C., and ω0 of 8.6 rad/sec.
A microporous polyethylene membrane was produced in the same manner as in Example 1 except for using a polyethylene composition comprising 30% by mass of UHMWPE having Mw of 2.2×106, 40% by mass of HDPE having Mw of 2.5×105, and 30% by mass of low-molecular-weight polyethylene (LMPE) having Mw of 2.0×103, which had T (60%) of 133.6° C., ΔTm of 13.7° C., and ω0 of 10.2 rad/sec, and changing the heat-setting temperature to 118° C.
The properties of the microporous polyethylene membranes obtained in Examples 1 to 4 and Comparative Examples 1 to 3 were measured by the following methods. The results are shown in Table 1.
(1) Average Thickness (μm)
The thickness of the microporous polyethylene membrane was measured at a 5-mm interval over a width of 30 cm by a contact thickness meter, and the measured thickness was averaged.
(2) Air Permeability (sec/100 cm3/20 μm)
The air permeability P1 of the microporous membrane having a thickness T1 was measured by an Oken-type air permeability meter (EGO-1T available from Asahi Seiko Co., Ltd.), and converted to air permeability P2 at a thickness of 20 μm by the formula of P2=(P1×20)/T1.
(3) Porosity (%)
It was measured by a mass method.
(4) Pin Puncture Strength (mN/20 μm)
The maximum load was measured when a microporous membrane having a thickness T1 was pricked with a needle of 1 mm in diameter with a spherical end surface (radius R of curvature: 0.5 mm) at a speed of 2 mm/second. The measured maximum load L1 was converted to the maximum load L2 at a thickness of 20 μm by the formula of L2=(L1×20)/T1, which was regarded as pin puncture strength.
(5) Tensile Rupture Strength and Elongation
Measurement was conducted on a 10-mm-wide rectangular test piece according to ASTM D882.
(6) Heat Shrinkage Ratio (%)
The shrinkage ratio of a microporous membrane was measured three times in both longitudinal direction (MD) and transverse direction (TD) after exposed to 105° C. for 8 hours, and averaged.
(7) Shutdown Temperature
The air permeability of a microporous polyethylene membrane was measured by an Oken-type air permeability meter (EGO-1T available from Asahi Seiko Co., Ltd.) while heating at a temperature-elevating speed of 5° C./minute, to find a temperature at which the air permeability reached the detection limit of 1×105 sec/100 cm3, which was regarded as a shutdown temperature (TSD).
(8) Air Permeability Change Ratio after Start of Shutdown
A temperature-air permeability curve as shown in
(9) Meltdown Temperature
After reaching the above shutdown temperature, heating was continued at a temperature-elevating speed of 5° C./minute, to find a temperature at which the air permeability became 1×105 sec/100 cm3 again, which was regarded as a meltdown temperature (TMD) (see
(1)Mw represents a mass-average molecular weight.
(2)A temperature at which the crystal-melting calorie ΔHm measured by DSC at a temperature-elevating speed of 10° C./minute reached 60% of the total ΔHm.
(3)A half-value of a melting endotherm curve obtained by DSC at temperature-elevating speed of 10° C./minute.
(4)An angular frequency at which the storage modulus (G′) and the loss modulus (G″) obtained by melt viscoelasticity measurement at a temperature of 180° C. were equal to each other.
(5)MD represents a longitudinal direction, and TD represents a transverse direction.
Table 1 shows that the microporous polyethylene membrane of Examples 1 to 4 had shutdown temperatures of 135° C. or lower, air permeability change ratios of 10,000 sec/100 cm3/° C. or more, and meltdown temperatures of 150° C. or higher, exhibiting low shutdown temperatures, high shutdown speeds and high meltdown temperatures. They further had excellent permeability, mechanical strength and heat shrinkage resistance. On the other hand, the membranes of Comparative Examples 1 and 2 having T (60%) of higher than 135° C. and ΔTm of higher than 10° C. had higher shutdown temperatures and poorer air permeability change ratios of less than 9,000 sec/100 cm3/° C. than those of Examples 1 to 4. Having ΔTm of higher than 10° C. and ω0 of more than 10 rad/sec, the membrane of Comparative Example 3 had a poorer air permeability change ratio of less than 9,000 sec/100 cm3/° C. and a lower meltdown temperature than those of Examples 1 to 4.
100 parts by mass of a polyethylene composition comprising 30% by mass of UHMWPE having Mw of 2.5×106 and 70% by mass of HOPE having Mw of 3.0×105 was dry-blended with 0.375 parts by mass of the above antioxidant Measurement revealed that the PE composition comprising UHMWPE and HDPE had T (20%) of 123.7° C., T (60%) of 133.2° C., and ω0 of 0.023 rad/sec (at 180° C.). A microporous polyethylene membrane was produced from the resultant mixture in the same manner as in Example 1 except for changing the simultaneous biaxial stretching temperature to 114° C.
A microporous polyethylene membrane was produced in the same manner as in Example 5 except for using a polyethylene composition comprising 20% by mass of UHMWPE and 80% by mass of HDPE, which had T (20%) of 123.3° C., T (60%) of 132.9° C., and ω0 of 0.025 rad/sec.
A microporous polyethylene membrane was produced in the same manner as in Example 5 except for using a polyethylene composition comprising 30% by mass of UHMWPE having Mw of 2.0×106 and 70% by mass of HDPE having Mw of 2.8×106, which had T (20%) of 124.5° C., T (60%) of 134.2° C., and ω0 of 0.69 rad/sec.
A microporous polyethylene membrane was produced in the same manner as in Example 5 except for using a polyethylene composition comprising 30% by mass of UHMWPE having Mw of 2.2×106 and 70% by mass of HDPE having Mw of 3.0×105, which had T (20%) of 126.1° C., T (60%) of 135.9° C., and ω0 of 2.1 rad/sec.
A microporous PE membrane was produced in the same manner as in Example 5 except for using a polyethylene composition comprising 30% by mass of UHMWPE having Mw of 2.2×106, 40% by mass of HDPE having Mw of 3.0×105, and 30% by mass of LMPE having Mw of 2.0×103, which had T (20%) of 122° C., T (60%) of 133.6° C., and ω0 of 10.2 rad/sec, and changing the heat-setting temperature to 117° C.
A microporous PE membrane was produced in the same manner as in Example 5 except for using a polyethylene composition comprising 30% by mass of UHMWPE having Mw of 2.2×106, 60% by mass of HDPE having Mw of 3.0×105, and 10% by mass of HDPE having Mw of 2.0×105, which had T (20%) of 124.3° C., T (60%) of 135.8° C., and ω0 of 10.3 rad/sec.
The microporous polyethylene membranes obtained in Examples 5 to 7 and Comparative Examples 4 to 6 were measured with respect to average thickness, air permeability, porosity, pin puncture strength, tensile rupture strength, tensile rupture elongation, heat shrinkage ratio, shutdown temperature, air permeability change ratio and meltdown temperature by the above methods. A curve shown in
(1)Mw represents a mass-average molecular weight.
(2)A temperature at which the crystal-melting calorie ΔHm measured by DSC at a temperature-elevating speed of 10° C./minute reached 20% of the total ΔHm.
(3)A temperature at which the crystal-melting calorie ΔHm measured by DSC at a temperature-elevating speed of 10° C./minute reached 60% of the total ΔHm.
(4)An angular frequency at which the storage modulus (G′) and the loss modulus (G″) obtained by melt viscoelasticity measurement at a temperature of 180° C. were equal to each other.
(5)MD represents a longitudinal direction, and TD represents a transverse direction.
As is clear from Table 2, the microporous polyethylene membranes of Examples 5 to 7 had shutdown temperatures of 135° C. or lower, air permeability change ratios of 1×104 sec/100 cm3/° C. or more, shutdown start temperatures of 130° C. or lower, meltdown temperatures of 155° C. or higher, exhibiting low shutdown start temperatures, high shutdown speeds, low shutdown temperatures, and high meltdown temperatures. They also had excellent permeability, mechanical strength and heat shrinkage resistance. On the other hand, the membrane of Comparative Example 4 having T (20%) of higher than 125° C. and T (60%) of higher than 135° C. had higher shutdown start temperature and shutdown temperature, and a poorer shutdown speed of less than 8,600 sec/100 cm3/° C. than those of Examples 5 to 7. Having ω0 of more than 1, the membranes of Comparative Examples 5 and 6 had poorer meltdown properties than those of Examples 5 to 7.
The first microporous polyolefin membrane of this invention has an excellent balance of a high air permeability change ratio after the start of shutdown, a low shutdown temperature, and meltdown properties, as well as excellent permeability, mechanical properties and heat shrinkage resistance. The second microporous polyolefin membrane of this invention has an excellent balance of low shutdown start temperature, a high air permeability change ratio after the start of shutdown, a low shutdown temperature, and meltdown properties. The use of the microporous polyolefin membrane of this invention for separators provides batteries with excellent stability, heat resistance, storage stability and productivity.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2005-318791 | Nov 2005 | JP | national |
| 2005-318792 | Nov 2005 | JP | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/JP2006/321759 | 10/31/2006 | WO | 00 | 4/30/2008 |
