JP2017162755A - Separator - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a separator which is high in melting point and strength, less in low-molecular weight component and superior in cleanness, and which can be shaped in a thin film form.SOLUTION: A separator comprises an ultra high molecular weight polyethylene composition including an ultra high molecular weight polyethylene having an intrinsic viscosity ([η]) of 10-80 dl/g, and 5-5000 pts.wt. of polyethylene to 100 pts.wt. of the ultra high molecular weight polyethylene. The polyethylene has a weight-average molecular weight(Mw) of 600,000 or less, a 210°C-melt tension of 100 mN or more, and a strain hardening property, of which the JIS K6760-compliant density is 935-960 kg/m.SELECTED DRAWING: None

Description

  The present invention relates to a separator made of a specific ultra-high molecular weight polyethylene composition, and more specifically, an ultra-high molecular weight having a high melting point and high strength, capable of being thinned, having low low molecular weight components and excellent cleanliness. The present invention relates to a polyethylene composition separator.

  The ultra high molecular weight ethylene polymer has an extremely high molecular weight corresponding to a viscosity average molecular weight (Mv) of 1 million or more, so that it has impact resistance, self-lubricity, abrasion resistance, weather resistance, chemical resistance It has excellent physical properties and dimensional stability, and has high physical properties comparable to engineering plastics. For this reason, application to applications such as lining materials, food industry line parts, machine parts, artificial joints, sporting goods, and microporous membranes has been attempted by various molding methods.

  However, ultra-high molecular weight ethylene polymer has extremely low fluidity when melted due to its high molecular weight, and it can be molded by kneading extrusion like ordinary polyethylene having a molecular weight in the range of tens of thousands to about 500,000. Have difficulty. Therefore, ultrahigh molecular weight polyethylene is a method of directly sintering polymer powder obtained by polymerization, a method of compression molding, a molding method by a ram extruder that extrudes while intermittently compressing, a state where it is dispersed in a solvent, etc. After extrusion molding, a method such as a method of removing the solvent is performed.

  Among these, in the molding method in which the solvent is removed after extrusion molding in a state dispersed in a solvent or the like, it is known that a porous film can be produced by uniaxial or biaxial stretching before and after removing the solvent. ing. The ultrahigh molecular weight polyethylene microporous membrane is expected to have excellent physical properties such as heat resistance, strength, and impact resistance due to the high molecular weight of ultra high molecular weight polyethylene. However, the ultra-high molecular weight polyethylene produced by the Ziegler catalyst currently on the market has a ratio of the weight average molecular weight (Mw) to the number average molecular weight (Mn) (molecular weight distribution) larger than 4, and the molecular weight distribution is wide. The strength and heat resistance of the molded body cannot be said to be sufficiently improved, and cannot be said to exhibit the expected performance.

  On the other hand, an ultrahigh molecular weight ethylene polymer having a narrow molecular weight distribution produced by using a metallocene catalyst or a post metallocene catalyst has also been proposed (see, for example, Patent Documents 1 and 2).

  Further, as a method for imparting stretchability to ultrahigh molecular weight polyethylene, a method of mixing low molecular weight polyethylene has been proposed (see, for example, Patent Document 3).

Japanese Patent No. 4868853 JP 2006-36988 A JP 2003-105121 A

  However, when a stretched microporous membrane is produced using the ultrahigh molecular weight polyethylene proposed in Patent Documents 1 and 2, since the moldability is poor, stretching is difficult and the performance is not sufficiently satisfactory. .

  Further, in the method proposed in Patent Document 3, since the polyethylene to be mixed for imparting stretchability contains many low molecular weight components, the composition obtained has many elutions of low molecular weight components, and there is a problem in cleanliness. In addition, it has a very high possibility of adversely affecting the mechanical strength characteristic of ultrahigh molecular weight polyethylene.

  Accordingly, an object of the present invention is to provide a separator made of an ultra-high molecular weight polyethylene composition that is excellent in mechanical strength, heat resistance, stretchability, and cleanliness.

  As a result of diligent research to solve the above problems, the present inventors have used a composition containing ultra-high molecular weight polyethylene and polyethylene having a specific molecular weight, melt tension, and strain-hardening property, thereby providing mechanical strength and heat resistance. It has been found that the separator can be excellent in properties and stretchability and excellent in cleanliness, and the present invention has been completed.

That is, according to the present invention, the weight average molecular weight (Mw) is 600,000 or less and the melt tension at 210 ° C. is 100 mN with respect to 100 parts by weight of ultrahigh molecular weight polyethylene having an intrinsic viscosity ([η]) of 10 dl / g to 80 dl / g. The ultrahigh molecular weight polyethylene composition having 5 to 5000 parts by weight of polyethylene having strain hardening property and density of 935 kg / m ³ or more and 960 kg / m ³ or less according to JIS K6760 It is related with the separator which consists of.

  The present invention is described in detail below.

The ultra high molecular weight polyethylene composition constituting the separator of the present invention has an Mw of 600,000 or less and a melt tension at 210 ° C. of 100 parts by weight of ultra high molecular weight polyethylene having [η] of 10 dl / g to 80 dl / g. It is a composition containing polyethylene having a strain hardening property and a density according to JIS K6760 of 935 kg / m ³ or more and 960 kg / m ³ or less at 100 mN or more.

  And as this ultra high molecular weight polyethylene composition, [η] of the ultra high molecular weight polyethylene composition is 0.9 times or less, especially 0.8 times or less of [η] of ultra high molecular weight polyethylene. A polyethylene composition is preferred.

  The ultrahigh molecular weight polyethylene constituting the ultrahigh molecular weight polyethylene composition may be any polymer as long as it belongs to the category called ultrahigh molecular weight polyethylene having [η] of 10 dl / g or more and 80 dl / g or less. Any ultrahigh molecular weight polyethylene prepared by a metallocene catalyst or the like may be used. Examples of ultra high molecular weight polyethylene include ultra high molecular weight ethylene homopolymer; ultra high molecular weight ethylene-propylene copolymer, ultra high molecular weight ethylene-1-butene copolymer, and ultra high molecular weight ethylene- And ultra high molecular weight ethylene-α-olefin copolymers such as 1-hexene copolymer and ultra high molecular weight ethylene-1-octene copolymer. Here, when [η] is less than 10 dl / g, the resulting composition is inferior in mechanical properties. On the other hand, when [η] exceeds 80 dl / g, the resulting composition is inferior in fluidity during molding, and particularly inferior in moldability when used as a separator. [Η] in the present invention is measured by a method of measuring at 135 ° C. with a polymer concentration of 0.0005 to 0.01% using decahydronaphthalene as a solvent, for example, using an Ubbelohde viscometer. Is possible.

  The ultra-high molecular weight polyethylene constituting the ultra-high molecular weight polyethylene composition may be anything as long as it belongs to the above category, and in particular, when it is used as a separator, it has mechanical strength, heat resistance, and stretchability. Metallocene ultrahigh molecular weight polyethylene is preferable because it is excellent and cleanliness is excellent, and ultra high molecular weight polyethylene described below or particles thereof are particularly preferable.

The ultra high molecular weight polyethylene has a particle shape because it has good fluidity of particles when used as a separator and has improved operability such as excellent filling rate in storage facilities, storage containers, and hoppers. are preferred, where the (2) bulk density 130 kg / ^{m 3} or more is preferably 700 kg / ^{m 3} or less and 200 kg / ^{m 3} or more from that becomes excellent particularly workability at the time of the separator 600 kg / m ³ or less is preferable. The bulk density can be measured by a method based on, for example, JIS K6760 (1995).

Since the ultrahigh molecular weight polyethylene is excellent in heat resistance, strength and the like when used as a separator, (1) 1st scan with a differential scanning calorimeter (hereinafter also referred to as DSC). Tm ₁ of the 1st scan at the time, then left for 5 minutes, then cooled to −20 ° C. at a temperature drop rate of 10 ° C./min, left for 5 minutes, and then again Tm ₂ of 2nd scan when 2nd scan was performed Measured, ΔTm = Tm ₁ -Tm ₂ is preferably 9 ° C. or higher and 30 ° C. or lower, particularly preferably 11 ° C. or higher and 30 ° C. or lower, and further excellent in heat resistance, mechanical strength, and moldability balance. ΔTm is preferably 11 ° C. or higher and 15 ° C. or lower because the separator is made of an ultrahigh molecular weight polyethylene composition.

In general polyethylene, an ethylene homopolymer belonging to high-density polyethylene is known as a polyethylene having a high melting point. However, the melting point of the high density polyethylene is as low as about 130 to 135 ° C. On the other hand, the ultra-high molecular weight polyethylene suitable for the separator of the present invention has an extremely high melting point (Tm) as compared with conventionally known polyethylene. For example, if it is an ethylene homopolymer, Tm ₁ has an extremely high melting point exceeding 140 ° C. In the ultra-high molecular weight polyethylene, the molecular chain of the polyethylene is highly crystallized, for example, so that ΔTm which is a difference between Tm ₁ and Tm ₂ when measured by DSC is 9 ° C. or more and 30 ° C. I think this will be a very big difference.

  Furthermore, the ultra high molecular weight polyethylene is capable of suppressing discoloration (yellowing) caused by titanium, oxidative deterioration, and the like, has a good color tone, and provides an ultra high molecular weight polyethylene composition having excellent weather resistance. In view of this, it is preferable that the titanium content is low, and in particular, the titanium content is preferably 0.02 ppm or less or the detection limit or less. The titanium content can be determined by chemical titration, measurement using a fluorescent X-ray analyzer, ICP emission analyzer, or the like.

Since the ultra high molecular weight polyethylene can provide a tougher separator, (4) Tm of 2nd scan measured by the above (3) after being heated and compressed at a press temperature of 190 ° C. and a press pressure of 20 MPa. It is preferable that the tensile strength at break (TS (MPa)) of the sheet formed by cooling at a mold temperature lower by 10 to 30 ° C. than ₂ satisfies the following relational expression (a). Since it is possible to provide a separator having excellent strength and wear resistance, it is preferable that the following relational expression (c) is satisfied.
TS ≧ 1.35 × Tm ₂ −130 (a)
1.35 × Tm ₂ −130 ≦ TS ≦ 2 × Tm ₂ −175 (c)
The tensile strength at break of general polyethylene is as low as about 45 MPa even with the highest density polyethylene. Further, conventional ultra-high molecular weight polyethylene has not been able to make full use of its high molecular weight, and the tensile strength at break was equivalent to that of general polyethylene, and did not exceed 50 MPa. For this reason, a method has been adopted in which the strength is increased by orientation by rolling at a high draw ratio.

  However, since the ultra high molecular weight polyethylene has moderately entangled polymer chains, [η] is 7 dl / g, preferably even in the ultra high molecular weight polyethylene region exceeding 15 dl / g. Even if it raises, tensile fracture strength does not fall, but rather shows the tendency to improve further. And, as the ultra high molecular weight polyethylene, when it is used as a separator, the strength is excellent. Therefore, if it belongs to the region of high density polyethylene, the tensile breaking strength measured by the above (4) is 40 MPa or more. It is preferable that it has, and, more preferably, it has 50 MPa or more.

  In addition, there is no restriction | limiting in particular as measurement conditions of tensile breaking strength, For example, test pieces, such as a strip shape and a dumbbell type | mold of thickness 0.1-5mm and width 1-50mm, are used for the tensile speed of 1 mm / min-500 mm / min. A method of measuring by speed can be exemplified.

Since the ultra-high molecular weight polyethylene has a relatively low content of low molecular weight components, enables moderate entanglement of polymer chains, and is a separator that is particularly excellent in heat resistance. The fracture stress (MTS (MPa)) when melt stretched at a temperature 20 ° C. higher than Tm _{2 of} the 2nd scan measured by (3) is preferably 1.5 MPa or more, and more preferably 2 MPa or more. It is preferable to have it.

  Note that general polyethylene having a molecular weight of 500,000 or less has high fluidity at a temperature 20 ° C. higher than the melting point (Tm), and the molded body is deformed by its own weight, so that it cannot be melt-stretched. In addition, the conventional ultrahigh molecular weight polyethylene can be melt-stretched even at a temperature 20 ° C. higher than the melting point (Tm), but strain hardening does not occur due to the low molecular weight component contained, and the stress remains low. In many cases, the fracture occurred due to a stress of about 1 MPa, resulting in poor heat resistance.

  And there is no restriction | limiting as a shaping | molding condition of the heat compression molding sheet | seat used for melt drawing, For example, it is the conditions of press temperature 100-250 degreeC and press pressure 5-50 MPa, Among them, especially the heat compression described in said (4). A molding method can be exemplified. Examples of the melt stretching method include a method of stretching a test piece such as a strip shape having a thickness of 0.1 to 5 mm and a width of 1 to 50 mm and a dumbbell shape at a tensile speed of 1 mm / min to 500 mm / min. be able to. Furthermore, as the rupture stress at the time of melt stretching, strain hardening occurs, if the stress increases with stretching, the maximum value is the rupture stress, strain hardening does not occur, and if the stress does not increase even after stretching, The stress in the flat region after yielding was taken as the breaking stress.

Since the ultra high molecular weight polyethylene is an ultra high molecular weight polyethylene composition having particularly excellent heat resistance, (6) the breaking stress (MTS (MPa)) and intrinsic viscosity (MTS (MPa)) measured by the above (5). [Η]) preferably satisfies the following relational expression (b), and particularly has excellent melt stretchability and moldability, and therefore satisfies the following relational expression (d). preferable.
MTS ≧ 0.079 × [η] (b)
0.079 × [η] ≦ MTS ≦ 0.23 × [η] (d)
The ultra-high molecular weight polyethylene is an ultra-high molecular weight polyethylene composition that is particularly excellent in fluidity as a powder and excellent in molding processability and physical properties. (7) Those having an average particle diameter of 1 μm or more and 1000 μm or less. preferable. The average particle size can be measured by a method such as a sieving test method using a standard sieve defined in JIS Z8801, for example.

  As the method for producing the ultra high molecular weight polyethylene, any method may be used, for example, a method for homopolymerization of ethylene, copolymerization of ethylene and other olefins using a catalyst for polyethylene production, Examples of the α-olefin at that time include propylene, 1-butene, 4-methyl-1-pentene, 1-hexene, 1-octene and the like. Examples of the polymerization method include a solution polymerization method, a bulk polymerization method, a gas phase polymerization method, a slurry polymerization method, and the like. Among them, it is possible to produce ultra high molecular weight polyethylene having a particularly uniform particle shape. Ultra high molecular weight polyethylene that can provide a separator made of an ultra high molecular weight polyethylene composition that has a high melting point, high crystallinity, and excellent mechanical strength, heat resistance, and wear resistance is efficiently and stably produced. Therefore, the slurry polymerization method is preferable. Further, the solvent used in the slurry polymerization method may be any organic solvent that is generally used, such as benzene, toluene, xylene, pentane, hexane, heptane, etc., and liquefied gas such as isobutane and propane, Olefins such as propylene, 1-butene, 1-octene and 1-hexene can also be used as a solvent.

  Further, as the polyethylene production catalyst used for producing the ultra high molecular weight polyethylene, any catalyst can be used as long as the ultra high molecular weight polyethylene can be produced. For example, at least the transition metal compound (A) And metallocene catalysts obtained from an organically modified clay (B) modified with an aliphatic salt and an organoaluminum compound (C).

  Examples of the transition metal compound (A) include a transition metal compound having a (substituted) cyclopentadienyl group and a (substituted) fluorenyl group, and a transition having a (substituted) cyclopentadienyl group and a (substituted) indenyl group. Metal compounds, transition metal compounds having a (substituted) indenyl group and a (substituted) fluorenyl group, etc. can be mentioned. Examples of the transition metal in this case include zirconium, hafnium, etc. Since it is possible to efficiently produce a molecular weight polyethylene, a zirconium compound having a (substituted) cyclopentadienyl group and an amino group-substituted fluorenyl group, and a (substituted) cyclopentadienyl group and an amino group-substituted fluorenyl group A hafnium compound is preferred.

  More specifically, for example, diphenylmethylene (1-indenyl) (9-fluorenyl) zirconium dichloride, diphenylmethylene (1-indenyl) (2,7-di-t-butyl-9-fluorenyl) zirconium dichloride, diphenyl Methylene (4-phenyl-1-indenyl) (2,7-di-t-butyl-9-fluorenyl) zirconium dichloride, diphenylsilanediyl (cyclopentadienyl) (2- (dimethylamino) -9-fluorenyl) zirconium Dichloride, diphenylsilanediyl (cyclopentadienyl) (2- (diethylamino) -9-fluorenyl) zirconium dichloride, diphenylsilanediyl (cyclopentadienyl) (2- (dibenzylamino) -9-fluorenyl) zyl Nium dichloride, diphenylsilanediyl (cyclopentadienyl) (2,7-bis (dimethylamino) -9-fluorenyl) zirconium dichloride, diphenylsilanediyl (cyclopentadienyl) (2,7-bis (diethylamino) -9 -Fluorenyl) zirconium dichloride, diphenylsilanediyl (cyclopentadienyl) (2,7-bis (dibenzylamino) -9-fluorenyl) zirconium dichloride, diphenylsilanediyl (cyclopentadienyl) (4- (dimethylamino) -9-fluorenyl) zirconium dichloride, diphenylsilanediyl (cyclopentadienyl) (4- (diethylamino) -9-fluorenyl) zirconium dichloride, diphenylsilanediyl (cyclopentadiyl) Nyl) (4- (dibenzylamino) -9-fluorenyl) zirconium dichloride, diphenylmethylene (cyclopentadienyl) (2- (dimethylamino) -9-fluorenyl) zirconium dichloride, diphenylmethylene (cyclopentadienyl) ( 2- (diethylamino) -9-fluorenyl) zirconium dichloride, diphenylmethylene (cyclopentadienyl) (2- (dibenzylamino) -9-fluorenyl) zirconium dichloride, diphenylmethylene (cyclopentadienyl) (2,7- Bis (dimethylamino) -9-fluorenyl) zirconium dichloride, diphenylmethylene (cyclopentadienyl) (2,7-bis (diethylamino) -9-fluorenyl) zirconium dichloride, diphenyl Methylene (cyclopentadienyl) (2,7-bis (dibenzylamino) -9-fluorenyl) zirconium dichloride diphenylmethylene (cyclopentadienyl) (4- (dimethylamino) -9-fluorenyl) zirconium dichloride, diphenylmethylene (Cyclopentadienyl) (4- (diethylamino) -9-fluorenyl) zirconium dichloride, diphenylmethylene (cyclopentadienyl) (4- (dibenzylamino) -9-fluorenyl) zirconium dichloride, diphenylmethylene (cyclopentadi) Enyl) (2,7-bis (dimethylamino) -9-fluorenyl) zirconium dichloride, diphenylmethylene (cyclopentadienyl) (2,7-bis (diethylamino) -9-fluorenyl) zyl Nium dichloride, diphenylmethylene (cyclopentadienyl) (2,7-bis (diisopropylamino) -9-fluorenyl) zirconium dichloride, diphenylmethylene (cyclopentadienyl) (2,7-bis (di-n-butyl- Amino) -9-fluorenyl) zirconium dichloride, diphenylmethylene (cyclopentadienyl) (2,7-bis (dibenzylamino) -9-fluorenyl) zirconium dichloride, diphenylmethylene (cyclopentadienyl) (3,6- Bis (dimethylamino) -9-fluorenyl) zirconium dichloride, diphenylmethylene (cyclopentadienyl) (3,6-bis (diethylamino) -9-fluorenyl) zirconium dichloride, diphenylmethylene (cyclope Tadienyl) (3,6-bis (di-n-propyl-amino) -9-fluorenyl) zirconium dichloride, diphenylmethylene (cyclopentadienyl) (2,5-bis (dimethylamino) -9-fluorenyl) zirconium dichloride Diphenylmethylene (cyclopentadienyl) (2,5-bis (diethylamino) -9-fluorenyl) zirconium dichloride, diphenylmethylene (cyclopentadienyl) (2,5-bis (diisopropylamino) -9-fluorenyl) zirconium Zirconium compounds such as dichloride; zirconium compounds obtained by converting these dichloro compounds to dimethyl, diethyl, dihydro, diphenyl, and dibenzyl compounds, and hafnium compounds obtained by converting zirconium of these compounds to hafnium A thing etc. can be illustrated.

  Examples of the organically modified clay (B) modified with the aliphatic salt include N, N-dimethyl-behenylamine hydrochloride, N-methyl-N-ethyl-behenylamine hydrochloride, N-methyl-Nn- Propyl-behenylamine hydrochloride, N, N-dioleyl-methylamine hydrochloride, N, N-dimethyl-behenylamine hydrofluoride, N-methyl-N-ethyl-behenylamine hydrofluoride, N- Methyl-Nn-propyl-behenylamine hydrofluorate, N, N-dioleyl-methylamine hydrofluoride, N, N-dimethyl-behenylamine hydrobromide, N-methyl-N- Ethyl-behenylamine hydrobromide, N-methyl-Nn-propyl-behenylamine hydrobromide, N, N-dioleyl-methylamine hydrobromide, N, N-dimethyl-be Nylamine hydroiodide, N-methyl-N-ethyl-behenylamine hydroiodide, N-methyl-Nn-propyl-behenylamine hydroiodide, N, N-dioleyl-methylamine iodide Hydronate, N, N-dimethyl-behenylamine sulfate, N-methyl-N-ethyl-behenylamine sulfate, N-methyl-Nn-propyl-behenylamine sulfate, N, N-dioleoyl-methyl Aliphatic amine salts such as amine sulfates; P, P-dimethyl-behenylphosphine hydrochloride, P, P-diethyl-behenylphosphine hydrochloride, P, P-dipropyl-behenylphosphine hydrochloride, P, P-dimethyl-behenyl Phosphine hydrofluoride, P, P-diethyl-behenylphosphine hydrofluoride, P, P-dipropyl-behenylphosphine fluoride Hydronate, P, P-dimethyl-behenylphosphine hydrobromide, P, P-diethyl-behenylphosphine hydrobromide, P, P-dipropyl-behenylphosphine hydrobromide, P, P- Dimethyl-behenylphosphine hydroiodide, P, P-diethyl-behenylphosphine hydroiodide, P, P-dipropyl-behenylphosphine hydroiodide, P, P-dimethyl-behenylphosphine sulfate, P , P-diethyl-behenylphosphine sulfate, and aliphatic phosphonium salts such as P, P-dipropyl-behenylphosphine sulfate;

Further, the clay compound constituting the organically modified clay (B) may be any clay compound as long as it belongs to the category of clay compounds, and generally a tetrahedron in which a silica tetrahedron is two-dimensionally continuous. A layer called a silicate layer formed by combining a sheet and an octahedron sheet in which an alumina octahedron, a magnesia octahedron, etc. are two-dimensionally continuous in a 1: 1 or 2: 1 layer is formed to overlap. Some of the silica tetrahedrons are replaced with the same type of Si by Al, alumina octahedron Al by Mg, magnesia octahedron Mg by Li, etc. It is known that cations such as Na ⁺ and Ca ²⁺ exist between the layers in order to compensate for this negative charge. As the clay compound, kaolinite, talc, smectite, vermiculite, mica, brittle mica, curdstone and the like as natural products or synthetic products exist, and these can be used. Smectite is preferable from the viewpoint of easiness of modification and organic modification, and hectorite or montmorillonite is more preferable among smectites.

  The organically modified clay (B) can be obtained by introducing the aliphatic salt between layers of the clay compound to form an ionic complex. In preparing the organically modified clay (B), it is preferable to carry out the treatment by selecting conditions of a clay compound concentration of 0.1 to 30% by weight and a treatment temperature of 0 to 150 ° C. The aliphatic salt may be prepared as a solid and dissolved in a solvent for use, or a solution of the aliphatic salt may be prepared by a chemical reaction in the solvent and used as it is. Regarding the reaction amount ratio between the clay compound and the aliphatic salt, it is preferable to use an aliphatic salt having an equivalent amount or more with respect to exchangeable cations of the clay compound. Examples of the processing solvent include aliphatic hydrocarbons such as pentane, hexane and heptane; aromatic hydrocarbons such as benzene and toluene; alcohols such as ethyl alcohol and methyl alcohol; ethers such as ethyl ether and n-butyl ether. Halogenated hydrocarbons such as methylene chloride and chloroform; acetone; 1,4-dioxane; tetrahydrofuran; water; Preferably, alcohols or water is used alone or as one component of a solvent.

  Moreover, there is no restriction | limiting in the particle size of the organic modified clay (B) which comprises the catalyst for polyethylene manufacture, and since it will become excellent in the efficiency at the time of catalyst preparation and the efficiency at the time of polyethylene manufacture among them, it may be 1-100 micrometers. preferable. There is no limitation on the method of adjusting the particle size at that time, and large particles may be pulverized to an appropriate particle size, small particles may be granulated to an appropriate particle size, or pulverization and granulation May be combined. The particle size may be adjusted on the clay before organic modification or on the organic modified clay after modification.

  Any organoaluminum compound (C) may be used as long as it belongs to the category called organoaluminum compound, and examples thereof include alkylaluminums such as trimethylaluminum, triethylaluminum, and triisobutylaluminum. Can do.

  The transition metal compound (A) (hereinafter also referred to as component (A)) constituting the catalyst for producing polyethylene, the organically modified clay (B) (hereinafter also referred to as component (B)), and The use ratio of the organoaluminum compound (C) (hereinafter sometimes referred to as component (C)) is not subject to any limitation as long as it can be used as a catalyst for polyethylene production. Since it becomes a polyethylene production catalyst capable of producing ultra-high molecular weight polyethylene with high production efficiency, the molar ratio of the component (A) to the component (C) per metal atom is (A) component: (C) component = It is preferably in the range of 100: 1 to 1: 100000, particularly preferably in the range of 1: 1 to 1: 10000. The weight ratio of the component (A) to the component (B) is preferably (A) component: (B) component = 10: 1 to 1: 10000, particularly in the range of 3: 1 to 1: 1000. It is preferable.

  Regarding the method for preparing the polyethylene production catalyst, any method may be used as long as it is possible to prepare the polyethylene production catalyst containing the component (A), the component (B) and the component (C). For example, there can be mentioned a method in which each of the components (A), (B) and (C) is mixed in an inert solvent or using a monomer for polymerization as a solvent. Moreover, there is no restriction | limiting also about the order which makes these components react, and the temperature and processing time which perform this process also have no restriction | limiting. It is also possible to prepare a catalyst for polyethylene production using two or more of each of the component (A), the component (B), and the component (C).

  Polymerization conditions such as a polymerization temperature, a polymerization time, a polymerization pressure, and a monomer concentration in producing the ultrahigh molecular weight polyethylene can be arbitrarily selected. Among them, a polymerization temperature of 0 to 100 ° C., a polymerization time of 10 seconds to 20 It is preferable to carry out in a range of time and polymerization pressure from normal pressure to 100 MPa. It is also possible to adjust the molecular weight using hydrogen during polymerization. The polymerization can be carried out by any of batch, semi-continuous and continuous methods, and can be carried out in two or more stages by changing the polymerization conditions. Further, the ultra-high molecular weight polyethylene obtained after completion of the polymerization can be obtained by separating and recovering from the polymerization solvent by a conventionally known method and drying it.

  Next, the polyethylene constituting the ultrahigh molecular weight polyethylene composition used for the separator of the present invention has an Mw of 600,000 or less, preferably 50,000 to 600,000, more preferably 100,000 to 600,000. Here, when Mw is polyethylene exceeding 600,000, the viscosity of the obtained composition becomes high, and molding becomes difficult.

  The polyethylene has a melt tension at 190 ° C. of 100 mN or more, preferably 150 mN or more. In addition, the polyethylene exhibits strain hardening in which (extension) viscosity increases rapidly with strain in uniaxial stretching or the like. By configuring the polyethylene having such characteristics, the separator of the present invention has a small variation in film thickness, and even with a thin film, the separator has a uniform film thickness.

The polyethylene has a density of 935 kg / m ³ or more and 960 kg / m ³ or less in accordance with JIS K6760. Here, when the density is less than 935 kg / m ³ , the resulting composition has low strength. On the other hand, if it exceeds 960 kg / m ³ , the resulting composition is brittle and inferior in handleability.

  And since this polyethylene becomes a separator which is excellent in strength and surface appearance when used as a separator, the ratio (Mw / Mn) of the weight average molecular weight to the number average molecular weight (hereinafter sometimes referred to as Mn) is 3. What is 0-8.0 is preferable.

  The polyethylene is produced, for example, by homopolymerizing ethylene or copolymerizing ethylene and the α-olefin exemplified above in the presence of a catalyst obtained by combining a transition metal complex called a metallocene catalyst and a specific promoter. be able to. The polyethylene is disclosed in JP-A-2004-346304, JP-A-2005-248013, JP-A-2006-2057, JP-A-2006-321991, JP-A-2007-169341, JP-A-2010-43152. What was obtained by methods, such as gazette, JP, 2011-89019, A JP, 2011-89020, A, may be sufficient.

  The ultrahigh molecular weight polyethylene composition constituting the separator of the present invention contains 5 parts by weight or more and 5000 parts by weight or less, preferably 20 parts by weight or more and 2000 parts by weight or less of the polyethylene with respect to 100 parts by weight of the ultrahigh molecular weight polyethylene. It will be. Here, when polyethylene is less than 5 weight part, it will be inferior to the moldability at the time of carrying out a separator. On the other hand, when it exceeds 5000 parts by weight, the separator obtained is inferior in mechanical strength and heat resistance.

  The ultra high molecular weight polyethylene composition constituting the separator of the present invention may be prepared by any method as long as the ultra high molecular weight polyethylene and polyethylene can be mixed to obtain an ultra high molecular weight polyethylene composition. For example, after extrusion kneading in a molten state, roll kneading, or dissolving in a solvent to form a solution, extrusion kneading, roll kneading, or stirring and mixing using a stirring blade, etc. Examples thereof include a method for removing the solvent by distillation, solvent extraction, and the like. Moreover, when melt | dissolving in an organic solvent, it can also be used for the mixed reaction with the organic solvent mentioned later to use the obtained mixture as it is. Examples of the solvent used here include linear or branched saturated or unsaturated aliphatic compounds such as hexane, heptane, decane, dodecane, tetradecane, octadecane, eicosane, liquid paraffin, and isoparaffin; cyclohexane, cyclodecane, and tetrahydronaphthalene. Saturated or unsaturated alicyclic compounds such as decahydronaphthalene; aromatic compounds such as benzene, toluene, xylene, naphthalene, anthracene; methylene chloride, 1,2-dichloroethane, 1,1,2-trichloroethane, chlorobenzene, And halogenated hydrocarbon compounds such as dichlorobenzene.

  The ultrahigh molecular weight polyethylene composition is a heat stabilizer, weather stabilizer, antistatic agent, antifogging agent, antiblocking agent, slip agent, lubricant, nucleating agent, pigment, etc., as long as it does not depart from the object of the present invention; Inorganic fillers or reinforcing agents such as carbon black, talc, glass powder, glass fiber, metal powder, etc .; organic fillers or reinforcing agents; flame retardants; known additives such as neutron shielding agents; Resins such as -1-butene, poly-4-methyl-1-pentene, ethylene / vinyl acetate copolymer, ethylene / vinyl alcohol copolymer, polystyrene, and these maleic anhydride grafts may be blended. The method of adding such additives includes ultra high molecular weight polyethylene, a method of blending with polyethylene, ultra high molecular weight polyethylene, polyethylene, and molding. It can be exemplified a method of blending, a method of preliminarily dry-blended or melt-blending, and the like to.

  The ultrahigh molecular weight polyethylene composition has excellent heat resistance and mechanical properties possessed by ultra high molecular weight polyethylene, has excellent processability possessed by polyethylene, and has excellent stretchability and cleanliness. Therefore, it is suitable for a separator.

The separator of the present invention is preferably a separator having a porosity of 10% or more and 80% or less, particularly 25% or more and 65% or less because it has an excellent balance between membrane strength and membrane resistance that affects permeability. In this case, the film thickness is preferably 0.001 to 1 mm, and the average pore diameter is preferably 1 to 1000 nm. The porosity in this case is, for example, porosity (V%) = 100−10 × (10 cm × 10 cm separator weight) (W, g) / (separator true density (g / cm ³ ) × separator film thickness ( d, mm)). Moreover, the film thickness (mm) of a separator can be calculated | required as an average value, for example, by measuring a film thickness with a contact-type film thickness meter at 30 points of the separator. The average pore diameter can be obtained by image analysis from an image obtained by observation with a scanning electron microscope in addition to the nitrogen adsorption method and the mercury intrusion method.

  The separator is particularly excellent in strength and can be made into a thin film. Therefore, the tensile strength at break measured at 23 ° C. is preferably 150 MPa or more. In particular, the heat shrinkage rate is preferably 2% or less because of excellent heat resistance, durability at high temperatures, and stability. In addition, the tensile breaking strength in this invention can be measured with a tensile tester etc., for example. Measurement conditions at that time can be measured, for example, by stretching a test piece having an initial length of 20 mm at a stretching speed of 10 to 100 mm / min. The thermal contraction rate can be measured by, for example, heating a 5 cm square microporous membrane at 100 ° C. for 1 hour, allowing to cool for 24 hours, and measuring the subsequent shrinkage rate.

  The method for producing the separator of the present invention is not particularly limited. For example, an ultrahigh molecular weight polyethylene composition and an organic solvent are mixed at a temperature of 50 ° C. or higher and 300 ° C. or lower to form a sheet, and then the organic material is converted from the sheet The method of attaching | subjecting the process of removing a solvent, and the process of giving biaxial stretching can be mentioned.

  Examples of the organic solvent in this case include high-boiling aliphatic hydrocarbons or alicyclic hydrocarbons such as octane, decane, dodecane, octadencan, decahydronaphthalene, and tetrahydronaphthalene; aromatics such as benzene, toluene, xylene, and naphthalene. Hydrocarbons: Halogenated hydrocarbons such as dichloroethane, trichloroethane, chlorobenzene, and trichlorobenzene; linear or branched liquid paraffin; paraffin wax; higher alcohols having 5 or more carbon atoms; phthalates, or mixtures thereof Can do. In addition, when the ultrahigh molecular weight polyethylene composition and the organic solvent are mixed, a separator having an excellent uniformity and smoothness can be obtained efficiently, so that the concentration of the ultrahigh molecular weight polyethylene composition is 0.5 wt% or more and 60 wt%. The content is preferably 5 wt% or more and 40 wt% or less. Then, when mixing the ultrahigh molecular weight polyethylene composition and the organic solvent, for example, a method of mixing in a reaction vessel equipped with a stirring blade, a method of extrusion kneading with a single-screw or twin-screw extruder, a reactor Examples of the method include extrusion kneading after the mixing. And the obtained mixture is shape | molded as a sheet-like material containing an organic solvent, for example by methods, such as compression molding, the extrusion method from T-die, a circular die, and inflation molding.

  Further, as the step of removing the organic solvent from the sheet-like material, for example, a drying method by heating, a method of drying after solvent extraction with a low melting point aliphatic or alicyclic hydrocarbon, alcohol, halogenated hydrocarbon, etc. Is mentioned.

  Examples of the biaxial stretching step include a simultaneous biaxial stretching method and a sequential biaxial stretching method in which sequential biaxial stretching is performed, and the stretching speed and stretching temperature at that time are constant. Alternatively, it may be multi-stage with change. The draw ratio is preferably 2 to 20 times in the longitudinal direction and 2 to 20 times in the transverse direction. The stretching temperature is preferably 0 ° C. or higher and 200 ° C. or lower. The order of the organic solvent removal step and the biaxial stretching step is arbitrary. For example, the biaxial stretching may be performed after the organic solvent is removed, or the organic solvent may be removed after the biaxial stretching. These may be performed simultaneously. Moreover, annealing can also be given after extending | stretching.

  The separator of the present invention can be used as, for example, a lithium battery separator, a lead storage battery separator, a nickel-cadmium storage battery separator, various battery separators for nickel-hydrogen batteries, an electrolytic cell separator, and the like, and is particularly suitable as a lithium secondary battery separator. It is a thing.

  The separator of the present invention is excellent in heat resistance, durability at high temperature, and stability, and when applied as a separator of a lithium ion secondary battery, it is not only reduced in size and weight by thinning, but also in an emergency. It is excellent in shutdown and safety, and is particularly suitable. And when using the separator of this invention as a separator of a lithium ion secondary battery, it is preferable that a film thickness shall be 15 micrometers or less.

In addition, when making a lithium ion secondary battery, the positive electrode can include lithium metal oxides such as cobalt, manganese and nickel composite oxide-lithium, and the cathode can include carbon materials such as graphite. Examples of the electrolytic solution may include an ethyl carbonate / diethyl carbonate solution of 1M LiPF ₆ . When these are applied to a lithium ion secondary battery, the lithium ion secondary battery in a charged state corresponding to 50% of the total capacity is set to 0.5 C (the discharge capacity of the lithium ion secondary battery is 2). 1C (current value for discharging the discharge capacity of the lithium ion secondary battery in 1 hour), 2C (current value for discharging the discharge capacity of the lithium ion secondary battery in 0.5 hour) After performing the corresponding constant current discharge for 10 seconds, the current was stopped, the voltage rise at that time was measured, and the DC resistance value calculated from the current value dependency (IR loss) of this voltage drop was 10 Ω · m ² or less, and When the lithium ion battery is charged and discharged at a constant current at a current value (0.5 C) for discharging in 2 hours, the separator is preferably a lithium ion secondary battery that can be charged and discharged 500 times or more.

  Since the separator of this invention is excellent in intensity | strength and heat resistance, it can be used as separators, such as a lithium ion battery (LiB), a lead storage battery, a nickel hydride battery, an alkaline battery.

  By providing a separator having a high melting point and high strength, low low molecular weight components, and excellent cleanliness and strength, it is possible to extend the continuous use time and reduce the size of the battery.

  Hereinafter, the present invention will be described in more detail with reference to examples, but the present invention is not limited to these examples.

  Unless otherwise noted, the reagents used were commercially available products or those synthesized according to known methods.

  A jet mill (manufactured by Seishin Enterprise Co., Ltd., (trade name) CO-JET SYSTEM α MARK III) was used for pulverizing the organically modified clay, and the particle size after pulverization was measured using a microtrack particle size distribution measuring device (manufactured by Nikkiso Co., Ltd., (Trade name) MT3000) was used to measure ethanol as a dispersant.

  Preparation of the catalyst for polyethylene production, production of polyethylene and solvent purification were all carried out in an inert gas atmosphere. A hexane solution (20 wt%) of triisobutylaluminum manufactured by Tosoh Finechem Co., Ltd. was used.

  Furthermore, various physical properties of the ultrahigh molecular weight polyethylene and polyethylene in the examples were measured by the following methods.

~ Measurement of intrinsic viscosity ([η]) ~
Using an Ubbelohde viscometer, measurement was conducted at 135 ° C. using decahydronaphthalene as a solvent at an ultrahigh molecular weight polyethylene concentration of 0.005 wt%.

~ Measurement of bulk density ~
It measured by the method based on JISK6760 (1995).

~ Measurement of Tm ₁ and Tm ₂ ~
Using DSC (product name: DSC6220, manufactured by SII NanoTechnology Co., Ltd.), the 1st scan was performed at a heating rate of 10 ° C./min, and the crystal melting peak (Tm ₁ ) of the 1st scan was measured. Thereafter, after standing for 5 minutes, the temperature was lowered to −20 ° C. at a rate of temperature drop of 10 ° C./min. After standing for 5 minutes, 2nd scan was performed again, and a crystal melting peak (Tm ₂ ) of 2nd scan was measured. The sample amount of ultra high molecular weight polyethylene at that time was 4 to 6 mg.

-Measurement of titanium content-
The ultra high molecular weight polyethylene was incinerated, alkali melted, and the prepared solution was used to determine the titanium content in the ultra high molecular weight polyethylene using an ICP emission analyzer (manufactured by PerkinElmer Co., Ltd., (trade name) Optima 3000XL). It was measured.

~ Measurement of average particle diameter ~
Obtained when classifying 100 g of ultrahigh molecular weight polyethylene particles using 9 types of sieves defined by JIS Z8801 (openings: 710 μm, 500 μm, 425 μm, 300 μm, 212 μm, 150 μm, 106 μm, 75 μm, 53 μm) The average particle diameter was determined by measuring the particle diameter at 50% weight on an integral curve obtained by integrating the weight of the particles remaining on each sieve from the side having a large opening.

~ Preparation of sheet for evaluation of ultra high molecular weight polyethylene particles ~
The evaluation sheet for ultrahigh molecular weight polyethylene particles was molded by the following method. That is, ultra high molecular weight polyethylene was sandwiched between polyethylene terephthalate films, preheated at 190 ° C. for 5 minutes, and then heat-rolled under conditions of 190 ° C. and a press pressure of 20 MPa. Thereafter, the mold was cooled at a mold temperature of 110 ° C. for 10 minutes to prepare a press sheet having a thickness of 0.3 mm.

~ Measurement of tensile strength at break ~
A sample cut into a dumbbell shape from a separator and an evaluation sheet for ultrahigh molecular weight polyethylene particles (measurement part width 5 mm) was allowed to stand at 23 ° C. for 48 hours, and then a tensile tester (A & D Co., Ltd.). (Trade name) Tensilon RTG-1210), a tensile test was performed at a measurement temperature of 23 ° C., an initial length of the test piece of 20 mm, and a tensile speed of 20 mm / min to obtain a tensile breaking strength.

-Measurement of breaking stress during melt drawing-
After the sample cut into a dumbbell shape from the separator and the evaluation sheet for ultrahigh molecular weight polyethylene particles by the method described in the measurement of tensile strength at break (10 mm in width of the measurement part) was left at 23 ° C. for 48 hours, Using a tensile tester (manufactured by A & D Co., Ltd., (trade name) Tensilon UMT2.5T), a tensile test is performed at 150 ° C. with an initial length of the test piece of 10 mm and a tensile speed of 20 mm / min. The breaking stress during stretching was determined. When strain hardening occurs and stress increases with stretching, the maximum value is the breaking stress, and when strain hardening does not occur and stress does not increase after stretching, the stress in the flat region after yielding is the breaking stress. did. In the microporous membrane, the value obtained by dividing the load by the apparent initial cross-sectional area was defined as stress.

-Weight average molecular weight (Mw), number average molecular weight (Mn), ratio of weight average molecular weight to number average molecular weight (Mw / Mn)-
The weight average molecular weight (Mw), the number average molecular weight (Mn), and the ratio of the weight average molecular weight to the number average molecular weight (Mw / Mn) were measured by GPC. The column temperature was set to 140 ° C. using a GPC device (trade name: HLC-8121 GPC / HT, manufactured by Tosoh Corporation) and a column (trade name: TSKgel GMHhr-H (20) HT, manufactured by Tosoh Corporation). The measurement was performed using 1,2,4-trichlorobenzene as an eluent. A measurement sample was prepared at a concentration of 1.0 mg / ml, and 0.3 ml was injected and measured. The calibration curve of molecular weight was calibrated using a polystyrene sample having a known molecular weight. In addition, Mw and Mn were calculated | required as a value of linear polyethylene conversion.

~ Measurement of melt tension ~
Capillograph (manufactured by Toyo Seiki Seisakusho) was used. A strand lowered at a piston descending speed of 10 mm / min was drawn at 10 m / min from a die having a length (L) of 8 mm and a diameter (D) of 2.095 mm at 210 ° C., and the take-up load was defined as melt tension.

~ Measurement of strain hardening ~
The measurement was performed using a Meissner type uniaxial extensional viscometer (manufactured by Toyo Seiki Seisakusho, trade name: Melten Rheometer) set at a temperature of 180 ° C. The non-linear parameter (λ) was obtained as a value obtained by dividing the maximum value of the extensional viscosity measured under the condition of strain rate of 0.07 to 0.1 s ⁻¹ by the extensional viscosity in the linear region at that time. In addition, the value of the extensional viscosity in the linear region is taken by Takeshi Fukuda, New Polymer Experimental Science 1, Basics of Polymer Experiment, Molecular Characteristic Analysis, “3-4. Molecular Shape and Form”, 295 (1994). According to the method described in the above, calculation was performed using an approximate expression from dynamic viscoelasticity. When the obtained λ exceeded 1, it was judged that there was strain hardening.

~density~
The density gradient tube method was used in accordance with JIS K6760 (1995).

~ Measurement of separator film thickness and porosity ~
The film thickness (d, mm) of the separator was determined by measuring the film thickness with a contact-type film thickness meter at 30 points of the microporous film, and taking the average value. The porosity (V,%) was calculated by measuring the weight (W, g) of a 10 cm × 10 cm microporous membrane, and calculating the true density (0.950 g / cm ³ ) of the porous membrane as shown below (e).

V = 100-W / 0.095d (e)
~ Measurement of separator pore distribution ~
After gold deposition, the surface of the microporous film was observed at a magnification of 10,000 times with a scanning electron microscope (manufactured by Keyence Co., Ltd., (trade name) VE-9800), and fine analysis was performed by image analysis of the obtained SEM photograph. The pore distribution was obtained, approximated to a geometric logarithmic distribution function, and the median diameter was taken as the average pore diameter.

~ Measurement of heat shrinkage ~
The heat shrinkage rate was calculated by calculating the rate of change in length and width after heating a 5 cm × 5 cm microporous membrane at 100 ° C. for 1 hour and allowing it to cool at room temperature for 24 hours.

-Evaluation of battery performance as secondary battery separator-
Laminate type lithium ion secondary battery using the obtained separator as a lithium ion secondary battery separator (positive electrode; cobalt-manganese-nickel composite oxide-lithium, cathode; graphite, electrolyte; 1M LiPF ₆ ethyl carbonate / diethyl A carbonate (= 1/1 vol%) solution, an electrode size: 4 mm × 4 mm, and a charging capacity of about 35 mA · h were prepared, and the performance was evaluated. The obtained lithium ion secondary battery was evaluated by measuring DC resistance and charge / discharge efficiency (= discharge capacity / charge capacity × 100) after three cycles of charge / discharge and adjusting the initial state. .
(DC resistance); 0.5C (current value for discharging the discharge capacity of the lithium ion secondary battery in 2 hours), 1C (lithium ion secondary battery) in a charged state corresponding to 50% of the total capacity The secondary battery was discharged for 10 seconds at a constant current corresponding to 2C (current value at which the discharge capacity of the lithium ion secondary battery was discharged at 0.5 hour). The voltage rise at that time was measured, and the DC resistance value was calculated from the current value dependence (IR loss) of this voltage drop. The measurement temperature is 25 ° C.
(Number of charge / discharge cycles): Charged to 4.2 V at a constant current of 0.5 C (current value for discharging the discharge capacity of the lithium ion secondary battery in 2 hours) at 25 ° C. Charging / discharging which discharged to 2.7V with a constant current was repeated, and the number of times the discharge capacity (C) was reduced to 60% of the initial discharge capacity was measured.

Production Example 1
(1) Preparation of organically modified clay Into a 1 liter flask was placed 300 ml of industrial alcohol (manufactured by Nippon Alcohol Sales, (trade name) Echinen F-3) and 300 ml of distilled water, 15.0 g of concentrated hydrochloric acid and dimethylbehenylamine (Lion After adding 42.4 g (120 mmol) of (trade name) Armin DM22D manufactured by Co., Ltd. and heating to 45 ° C., 100 g of synthetic hectorite (Rockwood Additives, (trade name) Laponite RDS) was dispersed. The mixture was heated to 60 ° C. and stirred for 1 hour while maintaining the temperature. The slurry was separated by filtration, washed twice with 600 ml of 60 ° C. water, and dried in an oven at 85 ° C. for 12 hours to obtain 125 g of an organically modified clay. This organically modified clay was pulverized by a jet mill to have a median diameter of 7 μm.

(2) Preparation of catalyst suspension for polyethylene production After replacing a 300 ml flask equipped with a thermometer and a reflux tube with nitrogen, 25.0 g of the organically modified clay obtained in (1) and 108 ml of hexane were added. Diphenylmethylene (cyclopentadienyl) (2- (diethylamino) -9-fluorenyl) hafnium dichloride (0.710 g) and 20% triisobutylaluminum (142 ml) were added, and the mixture was stirred at 60 ° C. for 3 hours. After cooling to 45 ° C., the supernatant was extracted, washed twice with 200 ml of hexane, and then 200 ml of hexane was added to obtain a suspension of a catalyst for producing polyethylene (solid weight: 11.5 wt%).

(3) Production of ultrahigh molecular weight polyethylene 1.2 liters of hexane, 1.0 ml of 20% triisobutylaluminum in a 2 liter autoclave, and 95.2 mg of the suspension of the catalyst for polyethylene production obtained in (2) (Equivalent to 10.9 mg of solid content) In addition, after the temperature was raised to 65 ° C., ethylene was continuously supplied so that the partial pressure became 1.3 MPa, and slurry polymerization of ethylene was performed. After 180 minutes, the pressure was released, and the slurry was filtered and dried to obtain 102 g of ultrahigh molecular weight polyethylene (1) (activity: 9360 g / g catalyst). The physical properties of the obtained ultrahigh molecular weight polyethylene (1) are shown in Table 1.

Production Example 2
(1) Preparation of organically modified clay Into a 1 liter flask, 300 ml of industrial alcohol (manufactured by Nippon Alcohol Sales Co., Ltd., (trade name) Echinen F-3) and 300 ml of distilled water were added, 15.0 g of concentrated hydrochloric acid and dioleylmethylamine (Lion Co., Ltd., (trade name) Armin M20) 64.2 g (120 mmol) was added and heated to 45 ° C. to disperse 100 g of synthetic hectorite (Rockwood Additives, (trade name) Laponite RDS). After that, the temperature was raised to 60 ° C. and stirred for 1 hour while maintaining the temperature. The slurry was separated by filtration, washed twice with 600 ml of water at 60 ° C., and dried in an oven at 85 ° C. for 12 hours to obtain 160 g of organically modified clay. This organically modified clay was pulverized by a jet mill to have a median diameter of 7 μm.

(2) Preparation of catalyst suspension for polyethylene production After replacing a 300 ml flask equipped with a thermometer and a reflux tube with nitrogen, 25.0 g of the organically modified clay obtained in (1) and 108 ml of hexane were added. Add 0.795 g of diphenylmethylene (4-phenyl-1-indenyl) (2,7-di-t-butyl-9-fluorenyl) zirconium dichloride and 142 ml of 20% triisobutylaluminum and stir at 60 ° C. for 3 hours. did. After cooling to 45 ° C., the supernatant was extracted, washed twice with 200 ml of hexane, and then 200 ml of hexane was added to obtain a suspension of a catalyst for producing polyethylene (solid weight: 11.3 wt%).

(3) Production of ultra-high molecular weight polyethylene 1.2 liters of hexane, 1.0 ml of 20% triisobutylaluminum in a 2 liter autoclave, 345 mg (solid) of the suspension for the catalyst for polyethylene production obtained in (2) (Corresponding to 38.9 mg / min), and the temperature was set to 45 ° C., and then ethylene was continuously supplied so that the partial pressure became 1.6 MPa to carry out slurry polymerization of ethylene. After 180 minutes, the pressure was released, and the slurry was filtered and dried to obtain 42.1 g of ultrahigh molecular weight polyethylene (2) (activity: 1080 g / g catalyst). The physical properties of the obtained ultrahigh molecular weight polyethylene (2) are shown in Table 1.

Production Example 3
(1) Preparation of organically modified clay The same procedure as in Production Example 1 was performed.

(2) Preparation of catalyst suspension for polyethylene production After replacing a 300 ml flask equipped with a thermometer and a reflux tube with nitrogen, 25.0 g of the organically modified clay obtained in (1) and 108 ml of hexane were added. Diphenylmethylene (cyclopentadienyl) (2- (dimethylamino) -9-fluorenyl) zirconium dichloride (0.593 g) and 20% triisobutylaluminum (142 ml) were added, and the mixture was stirred at 60 ° C. for 3 hours. After cooling to 45 ° C., the supernatant was taken out, washed twice with 200 ml of hexane, and then 200 ml of hexane was added to obtain a suspension of a catalyst for producing polyethylene (solid weight: 12.5 wt%).

(3) Production of ultrahigh molecular weight polyethylene 1.2 liters of hexane, 1.0 ml of 20% triisobutylaluminum in a 2 liter autoclave, 93.5 mg of the suspension for the catalyst for polyethylene production obtained in (2) (Equivalent to 11.7 mg of solid content) was added, and after raising the temperature to 50 ° C., 1.0 g of 1-butene was added, and ethylene was continuously supplied so that the partial pressure became 1.1 MPa, and slurry polymerization was performed. After 180 minutes, the pressure was released, and the slurry was filtered and dried to obtain 72.3 g of ultrahigh molecular weight polyethylene (3) (activity: 6180 g / g catalyst). Table 1 shows the physical properties of the obtained ultrahigh molecular weight polyethylene (3).

Production Example 4
(1) Preparation of organically modified clay and (2) Preparation of suspension of catalyst for polyethylene production were carried out in the same manner as in Production Example 3.

(3) Production of ultrahigh molecular weight polyethylene particles 1.2 liters of hexane, 1.0 ml of 20% triisobutylaluminum in a 2 liter autoclave, and 102 mg of a suspension of the catalyst for polyethylene production obtained in (2) ( (Equivalent to 12.8 mg of solid content), and after raising the temperature to 60 ° C., a hydrogen / ethylene mixed gas containing 150 ppm of hydrogen is supplied so that the partial pressure becomes 1.2 MPa, and then the partial pressure becomes 1.3 MPa. Thus, ethylene was continuously supplied to carry out slurry polymerization. After 210 minutes, the pressure was released, and the slurry was filtered and dried to obtain 88.2 g of ultrahigh molecular weight polyethylene (4) (activity: 6900 g / g catalyst). The physical properties of the obtained ultrahigh molecular weight polyethylene (4) are shown in Table 1.

製造例５
（１）固体触媒成分の調製は、製造例４と同様に実施した。

Production Example 5
(1) The solid catalyst component was prepared in the same manner as in Production Example 4.

(2) Preparation of catalyst suspension for polyethylene production After replacing a 300 ml flask equipped with a thermometer and a reflux tube with nitrogen, 25.0 g of the organically modified clay obtained in (1) and 108 ml of hexane were added. 0.427 g of dimethylsilylene (cyclopentadienyl) (4,7-dimethyl-1-indenyl) zirconium dichloride and 142 ml of 20% triisobutylaluminum were added and stirred at 60 ° C. for 3 hours. After cooling to 45 ° C., the supernatant was extracted, washed twice with 200 ml of hexane, and then 200 ml of hexane was added to obtain a suspension of a catalyst for producing polyethylene (solid weight: 11.5 wt%).

(3) Production of polyethylene 1.2 liters of hexane and 1.0 ml of 20% triisobutylaluminum in a 2 liter autoclave, 132 mg of a suspension of the catalyst for polyethylene production obtained in (2) (solid content 15. 2 mg equivalent), and after raising the temperature to 70 ° C., 0.1 g of butene is added. Further, ethylene is supplied so that the partial pressure becomes 1.2 MPa, and then the partial pressure becomes 1.2 MPa. Ethylene was continuously supplied to carry out slurry polymerization. After 180 minutes, the pressure was released, and the slurry was filtered and dried to obtain 71.7 g of polyethylene (5) (activity: 4720 g / g catalyst). Table 2 shows the physical properties of the obtained polyethylene (5).

Production Example 6
(1) Preparation of solid catalyst component, (2) Preparation of suspension of catalyst for polyethylene production was carried out in the same manner as in Production Example 5.

(2) Production of polyethylene 1.2 liters of hexane, 1.0 ml of 20% triisobutylaluminum in a 2 liter autoclave, and 250 mg of a suspension of the catalyst for production of polyethylene obtained in (2) (solid content 28. 8 mg equivalent), and after raising the temperature to 55 ° C., 0.15 g of butene is added. Further, ethylene is supplied so that the partial pressure becomes 1.2 MPa, and then the partial pressure becomes 1.2 MPa. Ethylene was continuously supplied to carry out slurry polymerization. After 180 minutes, the pressure was released, and the slurry was filtered and dried to obtain 82.1 g of polyethylene (6) (activity: 2860 g / g catalyst). Table 2 shows the physical properties of the obtained polyethylene (6).

Production Example 7
(1) The solid catalyst component was prepared in the same manner as in Production Example 4.

(2) Preparation of catalyst suspension for polyethylene production After replacing a 300 ml flask equipped with a thermometer and a reflux tube with nitrogen, 25.0 g of the organically modified clay obtained in (1) and 108 ml of hexane were added. Dimethylsilylene (cyclopentadienyl) (2,4,7-trimethyl-1-indenyl) zirconium dichloride (0.441 g) and 20% triisobutylaluminum (142 ml) were added, and the mixture was stirred at 60 ° C. for 3 hours. After cooling to 45 ° C., the supernatant was taken out, washed twice with 200 ml of hexane, and then 200 ml of hexane was added to obtain a suspension of a catalyst for producing polyethylene (solid weight: 12.3 wt%).

(3) Production of polyethylene 1.2 liters of hexane, 1.0 ml of 20% triisobutylaluminum in a 2 liter autoclave, and 325 mg (solid content of 40. 5 ml) of the catalyst for the production of polyethylene obtained in (2). 0 mg equivalent), and after raising the temperature to 50 ° C., 0.5 g of butene is added, ethylene is further supplied so that the partial pressure becomes 1.2 MPa, 0.15 g of butene is added, and then the partial pressure is reduced. Ethylene was continuously supplied so that the partial pressure became 1.2 MPa, and slurry polymerization was performed. After 180 minutes, the pressure was released, the slurry was filtered, and dried to obtain 83.2 g of polyethylene (7) (activity: 2080 g / g catalyst). Table 2 shows the physical properties of the obtained polyethylene (7).

Production Example 8
(1) Preparation of solid catalyst component In a 1 liter glass flask equipped with a thermometer and a reflux tube, 50 g (2.1 mol) of metal magnesium powder and 210 g (0.62 mol) of titanium tetrabutoxide were added. Then, 320 g (4.3 mol) of n-butanol in which 0.5 g was dissolved was added at 90 ° C. over 2 hours, and the mixture was further stirred at 140 ° C. for 2 hours under a nitrogen seal while excluding generated hydrogen gas to obtain a homogeneous solution. . Then 2100 ml of hexane was added.

  90 g of this component (equivalent to 0.095 mol of magnesium) was put in a separately prepared 500 ml glass flask and diluted with 59 ml of hexane. A hexane solution (106 ml) containing isobutylaluminum dichloride (0.29 mol) at 45 ° C. was added dropwise over 2 hours and further stirred at 70 ° C. for 1 hour to obtain a solid catalyst component. Remaining unreacted products and by-products were removed by decantation using hexane, and the composition was analyzed. The titanium content was 8.6 wt%.

(2) Production of polyethylene 1.2 liters of hexane, 1.0 ml of 20% triisobutylaluminum, and 8.3 mg of the solid catalyst component obtained in (1) were added to a 2 liter autoclave, and the temperature was raised to 80 ° C. Then, hydrogen was supplied at 0.08 MPa, and ethylene was continuously supplied at a partial pressure of 0.6 MPa. After 90 minutes, the pressure was released, and the slurry was filtered and dried to obtain 195 g of polyethylene (8) (activity: 23500 g / g catalyst). Table 2 shows the physical properties of the obtained polyethylene (8).

実施例１
製造例１で製造した超高分子量ポリエチレン（１）１．４ｇ、製造例５で製造したポリエチレン（５）１２．６ｇ、及び、流動パラフィン（ＭＯＲＥＳＣＯ社製、（商品名）モレスコホワイトＰ−３５０Ｐ）５６ｇ、酸化防止剤として、（商品名）Ｉｒｇａｎｏｘ１０１０（ＢＡＳＦ製）０．１３ｇ、（商品名）Ｉｒｇａｆｏｓ１６８（ＢＡＳＦ製）０．１３ｇを、１００ｃｃのバッチ式混練機（（株）東洋精機製作所製、（商品名）ラボプラストミル４Ｃ１５０）で、混練温度１９０℃、回転数５０ｒｐｍにて、１０分間混練し、得られた混合物を圧縮成形し、厚さ０．６ｍｍのシート状物とした。

Example 1
1.4 g of ultrahigh molecular weight polyethylene (1) produced in Production Example 1, 12.6 g of polyethylene (5) produced in Production Example 5, and liquid paraffin (MORESCO, (trade name) Moresco White P-350P ) 56 g, (Product name) Irganox 1010 (BASF) 0.13 g, (Product name) Irgafos 168 (BASF) 0.13 g as a 100 cc batch kneader (Toyo Seiki Seisakusho, (Trade name) Labo Plast Mill 4C150) and kneading for 10 minutes at a kneading temperature of 190 ° C. and a rotation speed of 50 rpm, and the resulting mixture was compression-molded to obtain a sheet-like material having a thickness of 0.6 mm.

  The sheet-like material is simultaneously biaxially stretched at 115 ° C. so that the set stretching ratio is 7 × 8 times in the longitudinal direction × lateral direction, washed with hexane, liquid paraffin is removed, and dried. Thus, a separator was manufactured.

  The obtained separator had no holes or tears that could be confirmed with the naked eye, and micropores were observed with an electron microscope. Table 3 shows the thickness of the separator, the standard deviation of the thickness, the porosity, the tensile strength at break, the thermal shrinkage, the direct current resistance of the battery when used for a lithium ion secondary battery separator, and the number of charge / discharge cycles.

Comparative Example 1
A separator was produced in the same manner as in Example 1 except that 2.1 g of ultrahigh molecular weight polyethylene (1) was changed to 14 g without using polyethylene (5).

  The load at the time of extending | stretching was high and it was not able to extend | stretch to a predetermined magnification.

Example 2
Instead of ultra high molecular weight polyethylene (1), 2.8 g of ultra high molecular weight polyethylene (2) produced in Production Example 2 and 11.2 g of polyethylene (6) produced in Production Example 6 instead of polyethylene (5) were used. An ultra-high molecular weight polyethylene composition and a separator were produced in the same manner as in Example 1 except that.

  The obtained separator had no holes or tears that could be confirmed with the naked eye, and micropores were observed with an electron microscope. Table 3 shows the thickness of the separator, the standard deviation of the thickness, the porosity, the tensile strength at break, the thermal shrinkage, the direct current resistance of the battery when used for a lithium ion secondary battery separator, and the number of charge / discharge cycles.

Comparative Example 2
A microporous membrane was produced in the same manner as in Example 2 except that polyethylene (6) was changed from 12.6 g to 14 g without using ultrahigh molecular weight polyethylene.

  The obtained film had no holes or tears that could be confirmed with the naked eye, and micropores were observed with an electron microscope. Table 3 shows the film thickness, the standard deviation of the film thickness, the porosity, the tensile strength at break, the thermal contraction rate, the direct current resistance of the battery when used for a lithium ion secondary battery separator, and the number of charge / discharge cycles. The tensile strength at break was small, the thermal shrinkage ratio was large, and there were elution components.

Comparative Example 3
A microporous membrane was produced in the same manner as in Example 2 except that polyethylene (8) produced in Production Example 8 was used instead of polyethylene (6).

  The obtained film had no holes or tears that could be confirmed with the naked eye, and micropores were observed with an electron microscope. Table 3 shows the film thickness, the standard deviation of the film thickness, the porosity, the tensile strength at break, the thermal contraction rate, the direct current resistance of the battery when used for a lithium ion secondary battery separator, and the number of charge / discharge cycles. The tensile strength at break was small, the thermal shrinkage ratio was large, and there were elution components.

Example 3
Instead of ultra high molecular weight polyethylene (1), 4.9 g of ultra high molecular weight polyethylene (3) produced in Production Example 3 and 9.1 g of polyethylene (7) produced in Production Example 7 instead of polyethylene (5) were used. Except for the above, an ultrahigh molecular weight polyethylene composition was obtained in the same manner as in Example 1 to prepare a sheet of ultrahigh molecular weight polyethylene mixture having a thickness of 0.9 mm. Further, a separator was manufactured in the same manner as in Example 1 with the set stretching ratio of 6 × 6 in the vertical direction × horizontal direction.

  The obtained separator had no holes or tears that could be confirmed with the naked eye, and micropores were observed with an electron microscope. Table 3 shows the thickness of the separator, the standard deviation of the thickness, the porosity, the tensile strength at break, the thermal shrinkage, the direct current resistance of the battery when used for a lithium ion secondary battery separator, and the number of charge / discharge cycles.

Example 4
Example 3 except that 7.7 g of the ultrahigh molecular weight polyethylene (4) produced in Production Example 4 was used instead of the ultrahigh molecular weight polyethylene (3), and the polyethylene (7) was changed to 6.3 g of polyethylene (6). In the same manner as above, an ultrahigh molecular weight polyethylene composition and a separator were produced.

  The obtained stretched porous film did not have holes or tears that could be confirmed with the naked eye, and micropores were observed with an electron microscope. Table 3 shows the thickness of the separator, the standard deviation of the thickness, the porosity, the tensile strength at break, the thermal shrinkage, the direct current resistance of the battery when used for a lithium ion secondary battery separator, and the number of charge / discharge cycles.

  The separator of the present invention is excellent in mechanical strength, heat resistance, stretchability and cleanliness, and is a lithium ion battery (LiB), a lead storage battery, a nickel metal hydride battery, and an alkaline battery. It can be used as a separator for an electrolytic cell or the like.

Claims (5)

For 100 parts by weight of ultrahigh molecular weight polyethylene having an intrinsic viscosity ([η]) of 10 dl / g or more and 80 dl / g or less, a weight average molecular weight (Mw) of 600,000 or less, a melt tension at 210 ° C. of 100 mN or more, and strain hardening A separator comprising an ultrahigh molecular weight polyethylene composition comprising 5 parts by weight or more and 5000 parts by weight or less of polyethylene having a density according to JIS K6760 and having a density of 935 kg / m ³ or more and 960 kg / m ³ or less. The separator according to claim 1, wherein the separator has a porosity of 10% or more and 80% or less. The separator according to claim 1 or 2, wherein a tensile breaking strength measured at 23 ° C is 150 MPa or more and a heat shrinkage rate is 2% or less. The melting point (Tm ₁ ) of the 1st scan when the ultra-high molecular weight polyethylene was heated from 0 ° C. to 230 ° C. (1st scan) at a heating rate of 10 ° C./min by DSC, then left for 5 minutes, The temperature was lowered to −20 ° C. at a temperature lowering rate of 10 ° C./min, left for 5 minutes, and then raised again from −20 ° C. to 230 ° C. (2nd scan) at a temperature rising rate of 10 ° C./min. Each of the melting points (Tm ₂ ) is measured, and the difference between the Tm ₁ and the Tm ₂ (ΔTm = Tm ₁ −Tm ₂ ) is an ultrahigh molecular weight polyethylene having a temperature of 9 ° C. or more and 30 ° C. or less. Item 4. The separator according to any one of Items 1 to 3. It is a separator of a lithium ion secondary battery, The separator in any one of Claims 1-4 characterized by the above-mentioned.