JP6779157B2 - Separator for non-aqueous secondary battery and non-aqueous secondary battery - Google Patents

Description

The present invention relates to a separator for a non-aqueous secondary battery and a non-aqueous secondary battery.

Non-aqueous secondary batteries represented by lithium ion secondary batteries are widely used as a power source for portable electronic devices such as notebook computers, mobile phones, digital cameras, and camcorders. With the miniaturization and weight reduction of portable electronic devices, the exterior of non-aqueous secondary batteries has been simplified and reduced in weight, and aluminum cans have been developed as exterior materials in place of stainless steel cans. In addition, aluminum laminated film packs have been developed to replace metal cans. However, since the aluminum laminated film pack is soft, in a battery using the pack as an exterior material (so-called soft pack battery), the electrode and the separator may be affected by an external impact or expansion and contraction of the electrode due to charge and discharge. Gap is likely to be formed between the batteries, which may reduce the cycle life of the battery.

In order to solve the above problems, a technique for enhancing the adhesion between the electrode and the separator has been proposed. As one of the techniques, a separator having a porous layer containing a polyvinylidene fluoride-based resin on a porous substrate is known (see, for example, Patent Document 1).

By the way, when manufacturing a battery, a laminate in which a separator is arranged between a positive electrode and a negative electrode may be subjected to a dry heat press (a heat press treatment performed without impregnating the separator with an electrolytic solution). If the separator and the electrode are adhered well by the dry heat press, it is possible to improve the manufacturing yield of the battery. However, the prior art as described in Patent Document 1 lacks the function of adhering to the electrode by dry heat pressing.

On the other hand, Patent Document 2 discloses a separator having an adhesive porous layer containing a mixture of polyvinylidene fluoride-based resin and acrylic-based resin on the surface of a porous base material. According to such a separator, the separator and the electrode are well adhered to each other by the dry heat press, so that the battery manufacturing yield is expected to be improved. However, when such a separator is used, a separator is placed between the positive electrode and the negative electrode and dry heat pressed, and then impregnated with an electrolytic solution, the acrylic resin swells or dissolves in the electrolytic solution. In some cases, the separator was easily peeled off from the electrode. In that case, even if the separator and the electrode are adhered by a dry heat press, a gap is formed between the separator and the electrode when the battery is actually immersed in the electrolytic solution, and as a result, the battery is used for a long period of time. The cycle life may be shortened when used in.

Japanese Patent No. 4127989 WO2016 / 98684

Against this background, the adhesiveness to the electrode by the dry heat press is good, and even when the electrolytic solution is impregnated after the adhesive by the dry heat press, the good adhesive state with the electrode is maintained. A separator is required.

The embodiments of the present disclosure have been made under the above circumstances.
The embodiment of the present disclosure is a separator provided with an adhesive porous layer containing a polyvinylidene fluoride-based resin, which has good adhesiveness to an electrode by a dry heat press, and is subsequently attached to the electrode even after being immersed in an electrolytic solution. An object of the present invention is to provide a separator for a non-aqueous secondary battery having excellent adhesiveness, and an object of the present invention is to solve this problem.

Specific means for solving the above problems include the following aspects.
[1] The adhesive porous layer comprises a porous base material and an adhesive porous layer provided on one or both sides of the porous base material and containing an acrylic resin and a polyvinylidene fluoride resin. It has a porous structure in which the acrylic resin and the polyvinylidene fluoride resin are mixed, and the total mass of the acrylic resin and the vinylidene polyvinylfluoride resin in the adhesive porous layer. On the other hand, the acrylic resin is contained in an amount of 2 to 40% by mass, and the acrylic resin contains 2-hydroxyethyl methacrylate, ethyl acrylate, butyl acrylate, methyl methacrylate, etc. as monomer components. A separator for a non-aqueous secondary battery, which is a ternary copolymer containing two types of acrylic monomers selected from the group consisting of polymethoxydiethylene glycol (meth) acrylate and a styrene monomer.
[2] The polyvinylidene fluoride-based resin is a copolymer containing vinylidene fluoride and hexafluoropropylene as monomer components, and the content of the hexafluoropropylene monomer component in the copolymer is 3% by mass. The separator for a non-aqueous secondary battery according to [1], wherein the content is ~ 20% by mass and the weight average molecular weight of the copolymer is 100,000 to 1.5 million.
[3] A positive electrode, a negative electrode, and a separator for a non-aqueous secondary battery according to any one of [1] to [2] arranged between the positive electrode and the negative electrode are provided, and lithium is doped / dedoped. A non-aqueous secondary battery that obtains electromotive force from the battery.

According to the present disclosure, it is a separator provided with an adhesive porous layer containing a polyvinylidene fluoride-based resin, which has good adhesiveness to an electrode by a dry heat press, and subsequently stays with the electrode even after being immersed in an electrolytic solution. A separator for a non-aqueous secondary battery having excellent adhesiveness is provided.

The embodiments of the present disclosure will be described below. These descriptions and examples exemplify the embodiments and do not limit the scope of the embodiments.

The numerical range indicated by using "~" in the present disclosure indicates a range including the numerical values before and after "~" as the minimum value and the maximum value, respectively.

In the present disclosure, the term "process" is included in this term not only as an independent process but also as long as the intended purpose of the process is achieved even if it cannot be clearly distinguished from other processes.

When referring to the amount of each component in the composition in the present disclosure, if a plurality of substances corresponding to each component are present in the composition, unless otherwise specified, the plurality of types present in the composition. It means the total amount of substances.

In the present disclosure, the "mechanical direction" means the long direction in the porous base material and the separator manufactured in a long shape, and the "width direction" means the direction orthogonal to the "mechanical direction". .. In the present disclosure, the "machine direction" is also referred to as the "MD direction", and the "width direction" is also referred to as the "TD direction".

As used herein, the "monomer component" of a copolymer means a component of the copolymer and a component unit formed by polymerizing the monomer.

<Separator for non-aqueous secondary batteries>
The separator for a non-aqueous secondary battery (also referred to as a "separator") of the present disclosure includes a porous base material and an adhesive porous layer provided on one side or both sides of the porous base material.

In the separator of the present disclosure, the adhesive porous layer has a porous structure in which an acrylic resin and a polyvinylidene fluoride resin are mixed. In this adhesive porous layer, the acrylic resin is contained in an amount of 2 to 40% by mass with respect to the total mass of the acrylic resin and the polyvinylidene fluoride-based resin. The acrylic resin is two kinds of acrylic monomers selected from the group consisting of 2-hydroxyethyl methacrylate, ethyl acrylate, butyl acrylate, methyl methacrylate, and polymethoxydiethylene glycol (meth) acrylate as monomer components. It is important that it is a tripolymer containing styrene monomer and styrene monomer.

Since the separator of the present disclosure is excellent in adhesion to the electrode by dry heat pressing, it is less likely to be misaligned with the electrode in the battery manufacturing process, and the battery manufacturing yield can be improved.
Further, the separator of the present disclosure is excellent in adhesion to an electrode by a dry heat press, and further, since a good adhesive state is maintained even after being immersed in an electrolytic solution, the cycle characteristics (capacity retention rate) of the battery are improved. Can be made to.
The reason for this is not clear, but it is presumed that the polarity derived from the acrylic group of the acrylic monomer has a great influence on the adhesion. On the other hand, since the styrene monomer has a low polarity, it is presumed to have an effect of suppressing dissolution and swelling in the electrolytic solution. With these combinations, the adhesiveness to the electrode by the dry heat press can be improved, and even when the adhesive porous layer is immersed in the electrolytic solution after being adhered by the dry heat press, excessive swelling of the adhesive porous layer can be suppressed, and the adhesive can be combined with the electrode. It is presumed that a good adhesive state is maintained. Further, such an acrylic resin has a high affinity with a polyvinylidene fluoride resin, both resins can be uniformly dissolved in a solvent, and a uniform adhesive porous layer can be easily formed. Then, the acrylic resin and the polyvinylidene fluoride-based resin are contained in the adhesive porous layer in a specific composition ratio, and both resins are uniformly dispersed at the molecular level, so that the adhesion between the separator and the electrode becomes uniform. , It is considered that it contributes to the improvement of the cycle characteristics of the battery.

Hereinafter, the details of the porous base material and the adhesive porous layer included in the separator of the present disclosure will be described.

[Porous substrate]
In the present disclosure, the porous base material means a base material having pores or voids inside. As such a base material, a microporous film; a porous sheet made of a fibrous material such as a non-woven fabric or paper; a composite porous structure in which one or more other porous layers are laminated on the microporous film or the porous sheet. Quality sheet; etc. As the porous base material, a microporous membrane is preferable from the viewpoint of thinning and strength of the separator. A microporous membrane means a membrane that has a large number of micropores inside and has a structure in which these micropores are connected so that a gas or liquid can pass from one surface to the other. To do.

As the material of the porous base material, a material having electrical insulation is preferable, and either an organic material or an inorganic material may be used.

The porous substrate preferably contains a thermoplastic resin in order to impart a shutdown function to the porous substrate. The shutdown function is a function of blocking the movement of ions by melting the constituent materials and closing the pores of the porous base material when the battery temperature rises to prevent thermal runaway of the battery. As the thermoplastic resin, a thermoplastic resin having a melting point of less than 200 ° C. is preferable. Examples of the thermoplastic resin include polyesters such as polyethylene terephthalate; polyolefins such as polyethylene and polypropylene; and the like, among which polyolefins are preferable.

As the porous base material, a microporous membrane containing polyolefin (referred to as "polyolefin microporous membrane") is preferable. Examples of the polyolefin microporous membrane include polyolefin microporous membranes applied to conventional battery separators, and it is preferable to select one having sufficient mechanical properties and ion permeability.

The polyolefin microporous membrane preferably contains polyethylene from the viewpoint of exhibiting a shutdown function, and the polyethylene content is preferably 95% by mass or more based on the total mass of the polyolefin microporous membrane.

The polyolefin microporous film is preferably a polyolefin microporous film containing polyethylene and polypropylene from the viewpoint of imparting heat resistance to the extent that the film does not easily break when exposed to a high temperature. Examples of such a polyolefin microporous membrane include a microporous membrane in which polyethylene and polypropylene are mixed in one layer. From the viewpoint of achieving both a shutdown function and heat resistance, the microporous membrane preferably contains 95% by mass or more of polyethylene and 5% by mass or less of polypropylene. Further, from the viewpoint of achieving both a shutdown function and heat resistance, a polyolefin microporous membrane having a laminated structure of two or more layers, at least one layer containing polyethylene and at least one layer containing polypropylene is also preferable.

As the polyolefin contained in the polyolefin microporous membrane, a polyolefin having a weight average molecular weight (Mw) of 100,000 to 5,000,000 is preferable. When the Mw of the polyolefin is 100,000 or more, sufficient mechanical properties can be imparted to the microporous membrane. On the other hand, when the Mw of the polyolefin is 5 million or less, the shutdown property of the microporous film is good, and the microporous film can be easily formed.

As a method for producing a polyolefin microporous film, a method in which a molten polyolefin resin is extruded from a T-die to form a sheet, which is crystallized and then stretched and then heat-treated to form a microporous film: liquid paraffin or the like. Examples thereof include a method in which a polyolefin resin melted together with a plasticizer is extruded from a T-die, cooled to form a sheet, stretched, and then the plasticizer is extracted and heat-treated to form a microporous film.

Examples of the porous sheet made of a fibrous material include polyesters such as polyethylene terephthalate; polyolefins such as polyethylene and polypropylene; heat-resistant resins such as aromatic polyamides, polyimides, polyethersulfones, polysulfones, polyetherketones and polyetherimides; celluloses. Examples thereof include porous sheets such as non-woven fabrics and papers made of fibrous materials such as. The heat-resistant resin refers to a resin having a melting point of 200 ° C. or higher, or a resin having no melting point and a decomposition temperature of 200 ° C. or higher.

Examples of the composite porous sheet include a sheet in which a functional layer is laminated on a porous sheet made of a microporous membrane or a fibrous material. Such a composite porous sheet is preferable from the viewpoint that further functions can be added by the functional layer. Examples of the functional layer include a porous layer made of a heat-resistant resin and a porous layer made of a heat-resistant resin and an inorganic filler from the viewpoint of imparting heat resistance. Examples of the heat-resistant resin include one or more heat-resistant resins selected from aromatic polyamide, polyimide, polyethersulfone, polysulfone, polyetherketone and polyetherimide. Examples of the inorganic filler include metal oxides such as alumina; metal hydroxides such as magnesium hydroxide; and the like. As a method of compounding, a method of applying a functional layer to a microporous membrane or a porous sheet, a method of joining a microporous membrane or a porous sheet and a functional layer with an adhesive, a method of joining a microporous membrane or a porous sheet with an adhesive, and a microporous membrane or a porous sheet. Examples thereof include a method of thermocompression bonding with the functional layer.

Even if various surface treatments are applied to the surface of the porous substrate for the purpose of improving the wettability with the coating liquid for forming the porous layer, as long as the properties of the porous substrate are not impaired. Good. Examples of the surface treatment include corona treatment, plasma treatment, flame treatment, and ultraviolet irradiation treatment.

[Characteristics of porous substrate]
In the present disclosure, the thickness of the porous substrate is preferably 5 μm to 25 μm from the viewpoint of obtaining good mechanical properties and internal resistance.

The gullet value (JIS P8117: 2009) of the porous substrate is preferably 50 seconds / 100 cc to 300 seconds / 100 cc from the viewpoint of suppressing a short circuit of the battery and obtaining sufficient ion permeability.

The porosity of the porous substrate is preferably 20% to 60% from the viewpoint of obtaining appropriate film resistance and shutdown function. The porosity of the porous substrate is determined according to the following calculation method. That is, the constituent materials are a, b, c, ..., N, the mass of each constituent material is Wa, Wb, Wc, ..., Wn (g / cm ² ), and the true density of each constituent material is da, When db, dc, ..., Dn (g / cm ³ ) and the film thickness is t (cm), the porosity ε (%) can be obtained from the following formula.
ε = {1- (Wa / da + Wb / db + Wc / dc + ... + Wn / dn) / t} × 100

The piercing strength of the porous base material is preferably 300 g or more from the viewpoint of improving the manufacturing yield of the separator and the manufacturing yield of the battery. The piercing strength of the porous substrate is measured by performing a piercing test using a KES-G5 handy compression tester manufactured by Kato Tech Co., Ltd. under the conditions of a radius of curvature of the needle tip of 0.5 mm and a piercing speed of 2 mm / sec. Refers to (g).

[Adhesive porous layer]
In the present disclosure, the adhesive porous layer is provided as the outermost layer of the separator on one side or both sides of the porous base material, and is a layer that adheres to the electrode when the separator and the electrode are overlapped and pressed or hot pressed.

In the present disclosure, the adhesive porous layer has a large number of micropores inside and has a structure in which these micropores are connected, so that gas or liquid can pass from one surface to the other. ing. In addition, the adhesive porous layer has a porous structure in which an acrylic resin and a polyvinylidene fluoride-based resin are mixed. Such a porous structure forms a fibril-like body in a state where the acrylic resin and the polyvinylidene fluoride-based resin are compatible or uniformly mixed at the molecular level, and a large number of such fibril-like bodies are integrally formed. It is a three-dimensional network structure that is connected. Such a porous structure can be confirmed by, for example, a scanning electron microscope (SEM) or the like.

It is preferable that the adhesive porous layer is present on both sides of the porous substrate rather than on only one side, from the viewpoint of excellent battery cycle characteristics. This is because when the adhesive porous layer is on both sides of the porous base material, both sides of the separator adhere well to both electrodes via the adhesive porous layer. In the present disclosure, the adhesive porous layer may further contain a resin other than the acrylic resin and the polyvinylidene fluoride resin, an inorganic filler, an organic filler, and the like, as long as the effects of the present invention are not impaired.

(Polyvinylidene fluoride resin)
In the present disclosure, the polyvinylidene fluoride-based resin contained in the adhesive porous layer is a homopolymer of vinylidene fluoride (that is, polyvinylidene fluoride); a copolymer of vinylidene fluoride and another copolymerizable monomer. (Polyvinylidene fluoride copolymer); a mixture thereof; Examples of the monomer copolymerizable with vinylidene fluoride include tetrafluoroethylene, hexafluoropropylene, trifluoroethylene, chlorotrifluoroethylene, vinyl fluoride, and trichlorethylene, and one or more of them may be used. Can be done. Of these, the VDF-HFP copolymer is preferable from the viewpoint of adhesiveness to the electrode. In addition, "VDF" here refers to a vinylidene fluoride monomer component, "HFP" refers to a hexafluoropropylene monomer component, and "VDF-HFP copolymer" refers to a VDF monomer component and It means a polyvinylidene fluoride-based resin having an HFP monomer component. By copolymerizing hexafluoropropylene with vinylidene fluoride, the crystallinity, heat resistance, solubility resistance in electrolytic solution, etc. of the polyvinylidene fluoride resin can be controlled within an appropriate range.

The separator of the present disclosure has an HFP monomer component content of 3% by mass to 20% by mass of all monomer components and a weight average molecular weight (Mw) of 100,000 to 1.5 million for the following reasons. It is preferable that the specific VDF-HFP copolymer is contained in the adhesive porous layer. Further, such a VDF-HFP copolymer is also preferable in that it has a high affinity with the acrylic resin.

When the HFP monomer component content of the VDF-HFP copolymer is 3% by mass or more, the mobility of the polymer chain when dry heat pressing is performed is high, and the polymer chain gets into the unevenness of the electrode surface and anchors. The effect can be exhibited and the adhesion of the adhesive porous layer to the electrode can be improved. From this viewpoint, the content of the HFP monomer component of the VDF-HFP copolymer is preferably 3% by mass or more, more preferably 5% by mass or more, and further preferably 6% by mass or more.
When the HFP monomer component content of the VDF-HFP copolymer is 20% by mass or less, it is difficult to dissolve in the electrolytic solution and does not swell excessively. Therefore, the electrode and the adhesive porous layer are formed inside the battery. Adhesion can be maintained. From this viewpoint, the HFP monomer component content of the VDF-HFP copolymer is preferably 20% by mass or less, more preferably 18% by mass or less, still more preferably 15% by mass or less.

When the Mw of the VDF-HFP copolymer is 100,000 or more, the mechanical properties of the adhesive porous layer that can withstand the bonding treatment with the electrode can be ensured, and the adhesion with the electrode can be improved. Further, when the Mw of the VDF-HFP copolymer is 100,000 or more, it is difficult to dissolve in the electrolytic solution, so that the adhesion between the electrode and the adhesive porous layer is easily maintained inside the battery. From these viewpoints, the Mw of the VDF-HFP copolymer is preferably 100,000 or more, more preferably 200,000 or more, further preferably 300,000 or more, still more preferably 500,000 or more.
When the Mw of the VDF-HFP copolymer is 1.5 million or less, the viscosity of the coating liquid used for coating molding of the adhesive porous layer does not become too high, and the moldability and crystal formation are good, and the adhesive porous The surface texture of the layer is highly uniform, and as a result, the adhesive porous layer adheres well to the electrode. Further, when the Mw of the VDF-HFP copolymer is 1.5 million or less, the mobility of the polymer chain when dry heat pressing is performed is high, and the polymer chain enters the unevenness of the electrode surface to exhibit the anchor effect. Adhesion of the adhesive porous layer to the electrode can be improved. From these viewpoints, the Mw of the VDF-HFP copolymer is preferably 1.5 million or less, more preferably 1.2 million or less, still more preferably 1 million or less.

Examples of the method for producing a PVDF or VDF-HFP copolymer include emulsion polymerization and suspension polymerization. It is also possible to select a commercially available VDF-HFP copolymer that satisfies the content of HFP units and the weight average molecular weight.

(Acrylic resin)
In the separator of the present disclosure, an acrylic resin is also contained in the adhesive porous layer in addition to the polyvinylidene fluoride resin. The acrylic resin contains two types of acrylic monomers selected from the group consisting of 2-hydroxyethyl methacrylate, ethyl acrylate, butyl acrylate, methyl methacrylate, and polymethoxydiethylene glycol (meth) acrylate as monomer components. , It is important that it is a ternary copolymer containing a styrene monomer.

Examples of the acrylic monomer constituting the acrylic resin include two types selected from the group consisting of 2-hydroxyethyl methacrylate, ethyl acrylate, butyl acrylate, methyl methacrylate, and polymethoxydiethylene glycol (meth) acrylate.

As the acrylic monomer, two types selected from the group consisting of methyl methacrylate, polymethoxydiethylene glycol (meth) acrylate, and n-butyl acrylate are preferable, and methacrylic acid having excellent compatibility with a polyvinylidene fluoride resin is particularly preferable. Most preferably, methyl methacrylate is contained because it has the effect of lowering the glass transition temperature of the adhesive porous layer.
On the other hand, since the acrylic resin of the present invention contains a styrene monomer as a constituent component, it is often partially compatible with the polyvinylidene fluoride-based resin. In such partial phase dissolution, the glass transition temperature of only the compatible portion is lowered, and the glass transition temperature of the incompatible portion before and after blending does not change. That is, in a binary copolymer such as methyl methacrylate and styrene monomer, a high glass transition temperature exceeding 100 ° C. may remain in part. As a result, it is considered that the fluidity of the adhesive porous layer is suppressed by the dry heat press, causing a decrease in the adhesive force. Lowering the glass transition temperature of the incompatible part with a binary copolymer of an acrylic monomer and a styrene monomer can be dealt with by using a long-chain alkyl-containing acrylic monomer, etc., but this may weaken the adhesive strength. Conceivable. In order to ensure the adhesive strength and lower the glass transition temperature of the incompatible portion, it is considered optimal to use two kinds of acrylic monomers.

The styrene monomer constituting the acrylic resin is an essential component of the acrylic resin because it has a strong effect of dissolving and suppressing swelling in the electrolytic solution.

In the separator of the present disclosure, the copolymerization ratio of the acrylic monomer and the styrene monomer (acrylic monomer / styrene monomer [mass ratio]) is 0.10 to 2.35 from the viewpoint of further improving the effect of the present invention. The range is preferable, more preferably 0.15 to 1.50, and even more preferably 0.20 to 1.00. When the copolymerization ratio of the acrylic monomer and the styrene monomer is 2.35 or less, it is difficult to peel off even when immersed in the electrolytic solution, which is preferable. On the other hand, when the copolymerization ratio of the acrylic monomer and the styrene monomer is 0.10 or more, the adhesive strength when dry heat pressing is easily improved, which is preferable.

The glass transition temperature of the acrylic resin used in the separator of the present disclosure is preferably in the range of −20 ° C. to 150 ° C. In general, the lower the glass transition temperature of an acrylic resin, the higher the fluidity of the adhesive porous layer during dry heat pressing. Therefore, polymer chains enter the irregularities on the surface of the electrode to exhibit the anchor effect, and the electrode Adhesive to Improves the adhesion of the porous layer to. On the other hand, even if the acrylic resin has a high glass transition, the glass transition temperature of the adhesive porous layer is substantially lowered when it is compatible with the vinylidene fluoride resin, for example, when it is completely or partially compatible. Therefore, it may develop high adhesive strength. When the glass transition temperature is −20 ° C. or higher, the adhesive porous layer located on the surface of the separator is less likely to cause blocking, which is preferable. When the glass transition temperature is 150 ° C. or lower, it is preferable because the adhesive effect by the dry heat press can be easily improved.

The Mw of the acrylic resin used in the separator of the present disclosure is preferably 10,000 to 500,000. When the Mw of the acrylic resin is 10,000 or more, it is preferable in that the adhesive strength with the electrode by the dry heat press is improved. On the other hand, when the Mw of the acrylic resin is 500,000 or less, the fluidity of the adhesive porous layer becomes good at the time of dry heat pressing, which is preferable. The more preferable range of Mw of the acrylic resin is 30,000 to 300,000, and more preferably the range of 50,000 to 200,000.

The content of the acrylic resin in the adhesive porous layer is the adhesive porous layer from the viewpoint of achieving the effect of the present invention and increasing the peel strength between the porous substrate and the adhesive porous layer. 2% by mass or more, more preferably 7% by mass or more, further preferably 10% by mass or more, and further preferably 15% by mass or more of the total amount of the total resin contained in. On the other hand, from the viewpoint of suppressing the cohesive destruction of the adhesive porous layer, the content of the acrylic resin in the adhesive porous layer is preferably 40% by mass or less of the total amount of the total resin contained in the adhesive porous layer. 38% by mass or less is more preferable, 35% by mass or less is further preferable, and 30% by mass or less is further preferable.

(Filler)
In the present disclosure, the adhesive porous layer may contain a filler made of an inorganic substance or an organic substance for the purpose of improving the slipperiness and heat resistance of the separator. In that case, it is preferable to set the content and particle size so as not to interfere with the effects of the present disclosure. As the filler, an inorganic filler is preferable from the viewpoint of improving cell strength and ensuring battery safety.

The average particle size of the filler is preferably 0.01 μm to 5 μm. The lower limit value is more preferably 0.1 μm or more, and the upper limit value is more preferably 1 μm or less.

As the inorganic filler, an inorganic filler that is stable with respect to the electrolytic solution and is electrochemically stable is preferable. Specifically, for example, metal hydroxides such as aluminum hydroxide, magnesium hydroxide, calcium hydroxide, chromium hydroxide, zirconium hydroxide, cerium hydroxide, nickel hydroxide, boron hydroxide; alumina, titania, magnesia, etc. Metal oxides such as silica, zirconia and barium titanate; carbonates such as calcium carbonate and magnesium carbonate; sulfates such as barium sulfate and calcium sulfate; clay minerals such as calcium silicate and talc; and the like can be mentioned. These inorganic fillers may be used alone or in combination of two or more. The inorganic filler may be surface-modified with a silane coupling agent or the like.

As the inorganic filler, at least one of metal hydroxide and metal oxide is preferable from the viewpoint of stability in the battery and ensuring the safety of the battery, and metal hydroxide is preferable from the viewpoint of imparting flame retardancy and eliminating static electricity. The material is preferable, and magnesium hydroxide is more preferable.

The particle shape of the inorganic filler is not limited and may be a shape close to a sphere or a plate shape, but from the viewpoint of suppressing a short circuit of the battery, the particle shape should be a plate shape particle or a non-aggregated primary particle. Is preferable.

When the adhesive porous layer contains an inorganic filler, the content of the inorganic filler in the adhesive porous layer is 5% by mass to 80% by mass of the total amount of the total resin and the inorganic filler contained in the adhesive porous layer. Mass% is preferable. When the content of the inorganic filler is 5% by mass or more, heat shrinkage of the separator is suppressed when heat is applied, which is preferable from the viewpoint of dimensional stability. From this point of view, the content of the inorganic filler is more preferably 10% by mass or more, further preferably 20% by mass or more. On the other hand, when the content of the inorganic filler is 80% by mass or less, it is preferable from the viewpoint of ensuring the adhesion of the adhesive porous layer to the electrode. From this point of view, the content of the inorganic filler is more preferably 80% by mass or less, and further preferably 75% by mass or less.

(Other ingredients)
In the present disclosure, the adhesive porous layer may contain additives such as a dispersant such as a surfactant, a wetting agent, a defoaming agent, and a pH adjuster. The dispersant is added to the coating liquid used for coating molding of the adhesive porous layer for the purpose of improving dispersibility, coatability and storage stability. Wetting agents, defoaming agents, and pH adjusters are used for coating liquids used for coating molding of adhesive porous layers, for example, for the purpose of improving compatibility with porous substrates, and air biting into the coating liquids. It is added for the purpose of suppressing crowding or adjusting the pH.

[Characteristics of adhesive porous layer]
In the present disclosure, the thickness of the adhesive porous layer is preferably 0.5 μm or more, more preferably 1.0 μm or more, and the energy density of the battery on one side of the porous substrate from the viewpoint of adhesiveness to the electrode. From the viewpoint of the above, 8.0 μm or less is preferable, and 6.0 μm or less is more preferable.

When the adhesive porous layer is provided on both sides of the porous substrate, the difference between the thickness of the adhesive porous layer on one surface and the thickness of the adhesive porous layer on the other surface is the sum of both sides. It is preferably 20% or less of the thickness of, and the lower the thickness, the more preferable.

The weight of the adhesive porous layer is preferably 0.5 g / m ² or more, more preferably 0.75 g / m ² or more, and ion permeability on one side of the porous substrate from the viewpoint of adhesiveness to the electrode. From the viewpoint of the above, 5.0 g / m ² or less is preferable, and 4.0 g / m ² or less is more preferable.

The porosity of the adhesive porous layer is preferably 30% or more from the viewpoint of ion permeability, preferably 80% or less, and more preferably 60% or less from the viewpoint of mechanical strength. The method for determining the porosity of the adhesive porous layer in the present disclosure is the same as the method for determining the porosity of the porous substrate.

The average pore size of the adhesive porous layer is preferably 10 nm or more from the viewpoint of ion permeability, and preferably 200 nm or less from the viewpoint of adhesiveness to the electrode. The average pore size of the adhesive porous layer in the present disclosure is calculated by the following formula, assuming that all the pores are columnar.
d = 4V / S
In the formula, d represents the average pore diameter (diameter) of the adhesive porous layer, V represents the pore volume per 1 m ² of the adhesive porous layer, and S represents the pore surface area per 1 m ² of the adhesive porous layer.
The pore volume V per 1 m ² of the adhesive porous layer is calculated from the pore ratio of the adhesive porous layer. The pore surface area S per 1 m ^{2 of the} adhesive porous layer is determined by the following method.
First, a specific surface area of the porous substrate (m 2 ^{/ g)} and specific surface area of the separator (m 2 ^{/ g),} by applying the BET equation to the nitrogen gas adsorption method, it is calculated from the nitrogen gas adsorption. Multiply these specific surface areas (m ² / g) by each basis weight (g / m ² ) to calculate the pore surface area per 1 m ^{2 of} each. Then, the pore surface area per 1 m ^{2 of the} porous substrate is subtracted from the pore surface area per 1 m ² of the separator to calculate the pore surface area S per 1 m ² of the adhesive porous layer.

The peel strength between the porous substrate and the adhesive porous layer is preferably 0.20 N / 10 mm or more. When the peel strength is 0.20 N / 10 mm or more, the handleability of the separator is excellent in the battery manufacturing process. From this point of view, the peel strength is more preferably 0.30 N / 10 mm or more, and the higher it is, the more preferable. The upper limit of the peel strength is not limited, but is usually 2.0 N / 10 mm or less.

[Characteristics of separator]
The thickness of the separator of the present disclosure is preferably 5 μm or more from the viewpoint of mechanical strength, and is preferably 35 μm or less from the viewpoint of the energy density of the battery.

The puncture strength of the separator of the present disclosure is preferably 250 g to 1000 g, more preferably 300 g to 600 g. The method for measuring the puncture strength of the separator is the same as the method for measuring the puncture strength of the porous substrate.

The porosity of the separator of the present disclosure is preferably 30% to 65%, more preferably 30% to 60%, from the viewpoint of adhesiveness to the electrode, handleability, ion permeability, and mechanical strength.

The galley value (JIS P8117: 2009) of the separator of the present disclosure is preferably 100 seconds / 100 cc to 300 seconds / 100 cc from the viewpoint of mechanical strength and battery load characteristics.

[Separator manufacturing method]
The separator of the present disclosure can be produced, for example, by a wet coating method having the following steps (i) to (iii).

(I) A step of applying a coating liquid containing a vinylidene fluoride resin and an acrylic resin to a porous substrate to form a coating layer.
(Ii) The porous base material on which the coating layer is formed is immersed in the coagulating liquid, and the polyvinylidene fluoride resin and the acrylic resin are solidified while inducing phase separation in the coating layer, and the porous base material is porous on the porous base material. The process of forming a layer and obtaining a composite film.
(Iii) A step of washing and drying the composite film with water.

The coating liquid is prepared by dissolving or dispersing a polyvinylidene fluoride resin and an acrylic resin in a solvent. When the adhesive porous layer contains a filler, the filler is dispersed in the coating liquid.

The solvent used for preparing the coating liquid contains a solvent that dissolves the polyvinylidene fluoride-based resin (hereinafter, also referred to as “good solvent”). Examples of the good solvent include polar amide solvents such as N-methylpyrrolidone, dimethylacetamide, dimethylformamide, and dimethylformamide.

The solvent used for preparing the coating liquid preferably contains a phase separation agent that induces phase separation from the viewpoint of forming a porous layer having a good porous structure. Therefore, the solvent used for preparing the coating liquid is preferably a mixed solvent of a good solvent and a phase separation agent. The phase separation agent is preferably mixed with a good solvent in an amount within a range in which an appropriate viscosity can be secured for coating. Examples of the phase separation agent include water, methanol, ethanol, propyl alcohol, butyl alcohol, butanediol, ethylene glycol, propylene glycol, tripropylene glycol and the like.

The solvent used for preparing the coating liquid is a mixed solvent of a good solvent and a phase separating agent from the viewpoint of forming a good porous structure, containing 60% by mass or more of the good solvent and 40% by mass of the phase separating agent. A mixed solvent containing% or less is preferable.

The resin concentration of the coating liquid is preferably 1% by mass to 20% by mass from the viewpoint of forming a good porous structure.

Examples of the means for applying the coating liquid to the porous substrate include a Meyer bar, a die coater, a reverse roll coater, a gravure coater and the like. When the porous layer is formed on both sides of the porous base material, it is preferable to apply the coating liquid to both sides at the same time from the viewpoint of productivity.

The coagulation liquid may be water alone, but generally contains water and the good solvent and phase separation agent used in the preparation of the coating liquid. It is preferable in terms of production that the mixing ratio of the good solvent and the phase separating agent is adjusted to the mixing ratio of the mixed solvent used for preparing the coating liquid. The content of water in the coagulation liquid is preferably 40% by mass to 90% by mass from the viewpoint of forming a porous structure and productivity. The temperature of the coagulant is, for example, 20 ° C to 50 ° C.

The separator of the present disclosure can also be manufactured by a dry coating method. In the dry coating method, a coating liquid containing a resin is applied to a porous substrate to form a coating layer, and then the coating layer is dried to solidify the coating layer and then onto the porous substrate. This is a method for forming a porous layer. However, since the porous layer tends to be denser in the dry coating method than in the wet coating method, the wet coating method is preferable from the viewpoint of obtaining a good porous structure.

The separator of the present disclosure can also be produced by producing a porous layer as an independent sheet, superimposing the porous layer on a porous base material, and laminating by thermocompression bonding or an adhesive. Examples of the method for producing the porous layer as an independent sheet include a method in which the above-mentioned wet coating method or dry coating method is applied to form a porous layer on the release sheet, and the release sheet is peeled from the porous layer. Be done.

<Non-water secondary battery>
The non-aqueous secondary battery of the present disclosure is a non-aqueous secondary battery that obtains an electromotive force by doping / dedoping lithium, and includes a positive electrode, a negative electrode, and a separator for the non-aqueous secondary battery of the present disclosure. Dope means occlusion, support, adsorption, or insertion, and means a phenomenon in which lithium ions enter the active material of an electrode such as a positive electrode.

The non-aqueous secondary battery of the present disclosure has, for example, a structure in which a battery element in which a negative electrode and a positive electrode face each other via a separator is enclosed in an exterior material together with an electrolytic solution. The non-aqueous secondary battery of the present disclosure is suitable for a non-aqueous electrolyte secondary battery, particularly a lithium ion secondary battery.

The non-aqueous secondary battery of the present disclosure has a high manufacturing yield because the separator of the present disclosure is excellent in adhesion to an electrode by a dry heat press.
In the non-aqueous secondary battery of the present disclosure, the separator of the present disclosure adheres firmly to the electrode by dry heat pressing, and the adhesiveness is maintained even in the subsequent immersion in the electrolytic solution. Therefore, the cycle characteristics (capacity retention rate) of the battery are maintained. ) Is excellent.

Hereinafter, examples of forms of the positive electrode, the negative electrode, the electrolytic solution, and the exterior material included in the non-aqueous secondary battery of the present disclosure will be described.

Examples of embodiments of the positive electrode include a structure in which an active material layer containing a positive electrode active material and a binder resin is arranged on a current collector. The active material layer may further contain a conductive additive. Examples of the positive electrode active material include lithium-containing transition metal oxides, specifically LiCoO ₂ , LiNiO ₂ , LiMn _1/2 Ni _1/2 O ₂ , LiCo _1/3 Mn _1/3 Ni _{1 /.} Examples thereof include ₃ O ₂ , LiMn ₂ O ₄ , LiFePO ₄ , LiCo _1/2 Ni _1/2 O ₂ , LiAl _1/4 Ni _3/4 O ₂ . Examples of the binder resin include polyvinylidene fluoride-based resins and styrene-butadiene copolymers. Examples of the conductive auxiliary agent include carbon materials such as acetylene black, ketjen black, and graphite powder. Examples of the current collector include aluminum foil, titanium foil, stainless steel foil and the like having a thickness of 5 μm to 20 μm.

In the non-aqueous secondary battery of the present disclosure, since the polyvinylidene fluoride resin contained in the adhesive porous layer of the separator of the present disclosure has excellent oxidation resistance, the adhesive porous layer is used as the positive electrode of the non-aqueous secondary battery. By arranging it on the side, LiMn _1/2 Ni _1/2 O ₂ , LiCo _1/3 Mn _1/3 Ni _1/3 O _2, etc. that can operate at a high voltage of 4.2 V or more can be used as the positive electrode active material. Easy to apply.

Examples of the embodiment of the negative electrode include a structure in which an active material layer containing a negative electrode active material and a binder resin is arranged on a current collector. The active material layer may further contain a conductive additive. Examples of the negative electrode active material include materials capable of electrochemically occluding lithium, and specific examples thereof include carbon materials; alloys of silicon, tin, aluminum and the like with lithium; wood alloys; and the like. Examples of the binder resin include polyvinylidene fluoride-based resins and styrene-butadiene copolymers. Examples of the conductive auxiliary agent include carbon materials such as acetylene black, ketjen black, graphite powder, and ultrafine carbon fibers. Examples of the current collector include copper foil, nickel foil, stainless steel foil and the like having a thickness of 5 μm to 20 μm. Further, instead of the above-mentioned negative electrode, a metallic lithium foil may be used as the negative electrode.

The electrolytic solution is a solution in which a lithium salt is dissolved in a non-aqueous solvent. Examples of the lithium salt include LiPF ₆ , LiBF ₄ , LiClO _{4, and the} like. Examples of the non-aqueous solvent include cyclic carbonates such as ethylene carbonate, propylene carbonate, fluoroethylene carbonate, difluoroethylene carbonate, and vinylene carbonate; and chain carbonates such as dimethyl carbonate, diethyl carbonate, ethylmethyl carbonate, and fluorine-substituted products thereof; Cyclic esters such as γ-butyrolactone and γ-valerolactone; may be used alone or in combination. As the electrolytic solution, the cyclic carbonate and the chain carbonate were mixed at a mass ratio (cyclic carbonate: chain carbonate) of 20:80 to 40:60, and the lithium salt was dissolved in 0.5 mol / L to 1.5 mol / L. The solution is suitable.

Examples of the exterior material include metal cans and aluminum laminated film packs. The shape of the battery includes a square shape, a cylindrical shape, a coin shape, and the like, and the separator of the present disclosure is suitable for any shape.

As a method for manufacturing a non-aqueous secondary battery of the present disclosure, a separator is subjected to a heat press treatment (referred to as "dry heat press" in the present disclosure) without impregnating the electrolyte solution to adhere to the electrode, and then to the separator. Examples thereof include a manufacturing method including impregnation with an electrolytic solution. The manufacturing method includes, for example, a laminating step of manufacturing a laminate in which the separator of the present disclosure is arranged between a positive electrode and a negative electrode, and a dry bonding step of performing a dry heat press on the laminate to bond the electrode and the separator. It has a post-process of injecting an electrolytic solution into a laminate housed in the exterior material and sealing the exterior material.

In the laminating step, the method of arranging the separator between the positive electrode and the negative electrode may be a method of laminating at least one layer of the positive electrode, the separator, and the negative electrode in this order (so-called stack method), and the positive electrode, the separator, the negative electrode, and the separator are laminated. A method of stacking them in order and winding them in the length direction may also be used.

The dry bonding step may be performed before accommodating the laminate in the exterior material (for example, a pack made of an aluminum laminate film), or may be performed after accommodating the laminate in the exterior material. That is, a laminate in which the electrodes and the separator are adhered by a dry heat press may be housed in the exterior material, and after the laminate is housed in the exterior material, a dry heat press is performed on the exterior material to separate the electrodes and the separator. It may be adhered.

The press temperature in the dry bonding step is preferably 70 ° C. to 120 ° C., more preferably 75 ° C. to 110 ° C., and even more preferably 80 ° C. to 100 ° C. In this temperature range, the adhesion between the electrode and the separator is good, and the separator can expand appropriately in the width direction, so that a short circuit of the battery is unlikely to occur.
The press pressure in the dry bonding step is preferably 0.5 kg to 40 kg as a load per 1 cm ² of the electrodes. The press time is preferably adjusted according to the press temperature and the press pressure, for example, in the range of 0.1 minutes to 60 minutes.

In the above manufacturing method, the laminate may be temporarily bonded by applying a normal temperature press (pressurization at room temperature) to the laminate before dry heat pressing.

In the post-process, after performing a dry heat press, the electrolytic solution is injected into the exterior material containing the laminate to seal the exterior material. After injecting the electrolytic solution, the laminate may be further heat-pressed from above the exterior material, but a good adhesive state can be maintained without heat-pressing. It is preferable that the inside of the exterior body is evacuated before sealing. Examples of the method of sealing the exterior material include a method of adhering the opening of the exterior material with an adhesive and a method of thermocompression bonding the opening of the exterior material by heating and pressurizing.

Hereinafter, the separator and the non-aqueous secondary battery of the present disclosure will be described in more detail with reference to examples. The materials, amounts used, proportions, treatment procedures, etc. shown in the following examples can be appropriately changed without departing from the spirit of the present disclosure. Therefore, the scope of the separators and non-aqueous secondary batteries of the present disclosure should not be construed as limiting by the specific examples shown below.

<Measurement method, evaluation method>
The measurement methods and evaluation methods applied in the examples and comparative examples are as follows.

[Composition of polyvinylidene fluoride resin]
20 mg of polyvinylidene fluoride-based resin was dissolved in 0.6 ml of deuterated dimethylsulfoxide at 100 ° C., a ¹⁹ F-NMR spectrum was measured at 100 ° C., and the composition of the polyvinylidene fluoride-based resin was determined from the NMR spectrum.

[Weight average molecular weight of resin]
For the weight average molecular weight (Mw) of the resin, a gel permeation chromatography analyzer (JASCO Corporation GPC-900) was used, two Tosoh TSKgel polystyrene AWM-Hs were used for the column, and N, N-dimethylformamide was used as the solvent. It was used and measured as a polystyrene-equivalent molecular weight under the conditions of a temperature of 40 ° C. and a flow rate of 10 ml / min.

[Resin glass transition temperature]
The glass transition temperature of the resin was determined from the differential scanning calorimetry curve (DSC curve) obtained by performing differential scanning calorimetry (DSC). The glass transition temperature is the temperature at which the straight line extending the baseline on the low temperature side to the high temperature side and the tangent line of the curve of the stepwise change portion and having the maximum gradient intersect.

[Film thickness of porous substrate and separator]
The film thickness (μm) of the porous base material and the separator was determined by measuring 20 points with a contact-type thickness meter (LITEMATIC manufactured by Mitutoyo Co., Ltd.) and averaging them. A columnar terminal having a diameter of 5 mm was used as the measurement terminal, and the measurement was adjusted so that a load of 7 g was applied during the measurement.

[Layer thickness of adhesive porous layer]
For the layer thickness (μm) of the adhesive porous layer, the total layer thickness of both sides was obtained by subtracting the film thickness of the porous base material from the film thickness of the separator, and half of this was taken as the layer thickness of one side.

[Gare value]
The galley value (seconds / 100cc) of the porous base material and the separator was measured using a galley type densometer (Toyo Seiki Co., Ltd. GB2C) according to JIS P8117: 2009.

[Vacancy rate]
The porosity (%) of the porous substrate and the adhesive porous layer was determined according to the following formula.
ε = {1-Ws / (ds · t)} × 100
In the formula, ε is the porosity (%), Ws is the basis weight (g / m ² ), ds is the true density (g / cm ³ ), and t is the thickness (μm).

[Peeling strength between the porous substrate and the adhesive porous layer]
Adhesive tape was attached to one surface of the separator (the length direction of the adhesive tape was made to match the MD direction of the separator), and the separator was cut out together with the adhesive tape in the TD direction 1.2 cm and the MD direction 7 cm. It was. The adhesive tape was slightly peeled off together with the adhesive porous layer directly underneath, and the two separated ends were gripped by Tensilon (RTC-1210A manufactured by Orientec Co., Ltd.) to perform a T-shaped peeling test. The adhesive tape is used as a support for peeling the adhesive porous layer from the porous substrate. The tensile speed of the T-shaped peeling test was 20 mm / min, and the load (N) when the adhesive porous layer was peeled from the porous substrate was measured. After the start of measurement, the load from 10 mm to 40 mm was collected at 0.4 mm intervals, the average was calculated, converted to the load per 10 mm width (N / 10 mm), and the measured values of the three test pieces were averaged. The peel strength was set to N / 10 mm.

[Adhesive strength with positive electrode: Dry heat press]
89.5 g of lithium cobalt oxide powder as a positive electrode active material, 4.5 g of acetylene black as a conductive aid, and 6 g of polyvinylidene fluoride as a binder were added to N-methyl so that the concentration of polyvinylidene fluoride was 6% by mass. -It was dissolved in pyroridene and stirred with a dual-arm mixer to prepare a slurry for positive electrodes. This positive electrode slurry was applied to one side of an aluminum foil having a thickness of 20 μm, dried, and pressed to obtain a positive electrode having a positive electrode active material layer.

The positive electrode obtained above was cut out to a width of 1.5 cm and a length of 7 cm, and the separator was cut out to 1.8 cm in the TD direction and 7.5 cm in the MD direction. The positive electrode and the separator were overlapped and hot-pressed under the conditions of a temperature of 80 ° C., a pressure of 5.0 MPa, and a time of 3 minutes to bond the positive electrode and the separator, and this was used as a test piece. At one end in the length direction of the test piece (that is, the MD direction of the separator), the separator is slightly peeled off from the positive electrode, and the two separated ends are gripped by Tensilon (RTC-1210A manufactured by Orientec) to perform a T-shaped peeling test. went. The tensile speed of the T-shaped peeling test was set to 20 mm / min, the load (N) when the separator peeled from the positive electrode was measured, and the load from 10 mm to 40 mm was collected at 0.4 mm intervals after the start of measurement, and the average was calculated. Then, the measured values of the three test pieces were averaged to obtain the adhesive strength (N) of the separator.

[Adhesion with positive electrode: after immersion in electrolytic solution]
The positive electrode and separator after dry heat press bonding obtained in the above [Adhesion strength with positive electrode] are placed in an electrolytic solution (1 mol / L LiPF ₆ -ethylene carbonate: ethyl methyl carbonate [mass ratio 3: 7]) at room temperature for 24 hours. After the immersion, it was taken out from the electrolytic solution, the separator was pinched by hand and peeled off from the positive electrode, and the adhesiveness after the electrolytic solution was immersed was confirmed according to the following criteria.
A: Strong adhesion (The separator does not fall off from the electrode just by reversing the sample, and it can be confirmed by microscopic observation after peeling that many adhesive porous layers are attached to the electrode surface).
B: Sufficient adhesion (The separator does not fall off from the electrode just by inverting the sample, and it can be confirmed by microscopic observation after peeling that a slight adhesive porous layer is attached to the electrode surface).
C: Weak adhesion (The separator does not come off from the electrode just by inverting the sample, but it can be easily peeled off by hand, and almost no adhesive porous layer remains on the electrode surface by microscopic observation after peeling).
D: No adhesion (the separator just flipped the sample and the separator fell off from the electrode, and the separator and electrode were not completely adhered).

[Adhesive strength with negative electrode]
Add 300 g of artificial graphite as a negative electrode active material, 7.5 g of a water-soluble dispersion containing 40% by mass of a modified styrene-butadiene copolymer as a binder, 3 g of carboxymethyl cellulose as a thickener, and an appropriate amount of water. The mixture was stirred with a formula mixer to prepare a slurry for the negative electrode. This negative electrode slurry was applied to one side of a copper foil having a thickness of 10 μm, dried and pressed to obtain a negative electrode having a negative electrode active material layer.

Using the negative electrode obtained above, a T-shaped peeling test was performed in the same manner as in the above [Adhesive strength with positive electrode: dry heat press] to determine the adhesive strength (N) of the separator.

[Adhesion with negative electrode: after immersion in electrolytic solution]
Using the negative electrode obtained above, the adhesiveness after immersion in the electrolytic solution was confirmed in the same manner as in the above [Adhesion with the positive electrode: after immersion in the electrolytic solution].

[Cycle characteristics (capacity retention rate)]
Lead tabs were welded to the positive electrode and the negative electrode, and the positive electrode, the separator, and the negative electrode were laminated in this order. This laminate is inserted into a pack made of aluminum laminate film, the inside of the pack is evacuated using a vacuum sealer and temporarily sealed, and the entire pack is hot-pressed using a hot press in the laminating direction of the laminate. As a result, the electrode and the separator were adhered to each other. The conditions for hot pressing were a temperature of 90 ° C., a load of 20 kg per 1 cm ^{2 of} electrodes, and a pressing time of 2 minutes. Next, an electrolytic solution (1 mol / L LiPF ₆ -ethylene carbonate: ethyl methyl carbonate [mass ratio 3: 7]) is injected into the pack, the laminate is impregnated with the electrolytic solution, and then the inside of the pack is used with a vacuum sealer. Was sealed in a vacuum state to obtain a battery.

The battery was charged and discharged for 500 cycles in an environment of a temperature of 40 ° C. Charging was 1C and 4.2V constant current constant voltage charging, and discharging was 1C and 2.75V cutoff constant current discharge. The discharge capacity at the 500th cycle was divided by the initial capacity, the average of 10 batteries was calculated, and the obtained value (%) was used as the capacity retention rate.

[Load characteristics]
A battery was manufactured in the same manner as the battery manufactured in the above [Cycle characteristics (capacity retention rate)]. In an environment of a temperature of 15 ° C., the batteries are charged and discharged, the discharge capacity when discharged at 0.2 C and the discharge capacity when discharged at 2 C are measured, the latter is divided by the former, and 10 batteries are used. The average was calculated and the obtained value (%) was used as the load characteristic. The charging condition was 0.2C, 4.2V constant current constant voltage charging for 8 hours, and the discharging condition was 2.75V cutoff constant current discharge.

<Making a separator>
[Example 1]
A polyvinylidene fluoride-based resin (VDF-HFP copolymer, HFP unit content 12.4% by mass) in a mixed solvent of dimethylacetamide and tripropylene glycol (dimethylacetamide: tripropylene glycol = 80: 20 [mass ratio]), Weight average molecular weight 860,000) and acrylic resin (methyl methacrylate (MMA) -butyl acrylate (BA) -styrene copolymer, polymerization ratio [mass ratio] 40:20:40, weight average molecular weight 144,000 , Glass transition temperature (64 ° C.)) to prepare a coating liquid for forming an adhesive porous body. The mass ratio of the polyvinylidene fluoride-based resin and the acrylic-based resin contained in the coating liquid was 80:20, and the resin concentration of the coating liquid was 5.0% by mass.

The coating liquid is applied to both sides of a polyethylene microporous film (thickness: 9.0 μm, galley value: 150 seconds / 100 cc, pore ratio: 43%), which is a porous base material (at that time, the amount of coating on the front and back sides). Was applied to equal amounts of water) and coagulated liquid (water: dimethylacetamide: tripropylene glycol = 62.5: 30: 7.5 [mass ratio], liquid temperature 35 ° C.) to solidify. .. Then, this was washed with water and dried to obtain a separator having an adhesive porous layer formed on both sides of the polyethylene microporous membrane.

[Example 2]
As an acrylic resin, methyl methacrylate (MMA) -butyl acrylate (BA) -styrene copolymer, polymerization ratio [mass ratio] 30:20:50, weight average molecular weight 156,000, glass transition temperature 67 ° C.) A separator was prepared in the same manner as in Example 1 except that it was changed to.

[Example 3]
As an acrylic resin, 2-hydroxyethyl methacrylate (2-HEMA) -butyl acrylate (BA) -styrene copolymer, polymerization ratio [mass ratio] 10:18:72, weight average molecular weight 115,000, glass A separator was prepared in the same manner as in Example 1 except that the transition temperature was changed to 71 ° C.).

[Example 4]
As an acrylic resin, 2-hydroxyethyl methacrylate (2-HEMA) -butyl acrylate (BA) -styrene copolymer, polymerization ratio [mass ratio] 17:11:72, weight average molecular weight 112,000, glass A separator was prepared in the same manner as in Example 1 except that the transition temperature was changed to 83 ° C.).

[Example 5]
As an acrylic resin, 2-hydroxyethyl methacrylate (2-HEMA) -ethyl acrylate (EA) -styrene copolymer, polymerization ratio [mass ratio] 10:18:72, weight average molecular weight 114,000, glass A separator was prepared in the same manner as in Example 1 except that the transition temperature was changed to 80 ° C.).

[Example 6]
As an acrylic resin, 2-hydroxyethyl methacrylate (2-HEMA) -ethyl acrylate (EA) -styrene copolymer, polymerization ratio [mass ratio] 30:12:58, weight average molecular weight 129,000, glass A separator was prepared in the same manner as in Example 1 except that the transition temperature was changed to 86 ° C.).

[Example 7]
As an acrylic resin, 2-hydroxyethyl methacrylate (2-HEMA) -ethyl acrylate (EA) -styrene copolymer, polymerization ratio [mass ratio] 34:18:48, weight average molecular weight 153,000, glass A separator was prepared in the same manner as in Example 1 except that the transition temperature was changed to 78 ° C.).

[Example 8]
As an acrylic resin, ethyl acrylate (EA) -methoxydiethylene glycol methacrylate (MDEGA, n = 9) -styrene copolymer, polymerization ratio [mass ratio] 10.5: 10: 79.5, weight average molecular weight 13.3 A separator was prepared in the same manner as in Example 1 except that the glass transition temperature was changed to 70 ° C.).

[Example 9]
As an acrylic resin, ethyl acrylate (EA) -methoxydiethylene glycol methacrylate (MDEGA, n = 9) -styrene copolymer, polymerization ratio [mass ratio] 5:20:75, weight average molecular weight 160,000, glass transition temperature 52 A separator was prepared in the same manner as in Example 1 except that the temperature was changed to (° C.).

[Example 10]
Magnesium hydroxide particles (volume average particle size of primary particles 0.8 μm, BET specific surface area 6.8 m ² / g) were further dispersed in the coating liquid so as to have the contents shown in Table 1. A separator was prepared in the same manner as in Example 1.

[Comparative Example 1]
A separator was prepared in the same manner as in Example 1 except that the coating liquid did not contain an acrylic resin.

[Comparative Example 2]
A separator was prepared in the same manner as in Example 1 except that the coating liquid did not contain an acrylic resin and the contents of the polyvinylidene fluoride-based resin and magnesium hydroxide particles were changed as shown in Table 1.

[Comparative Example 3]
Acrylic resin contained in the coating liquid is a methyl methacrylate (MMA) -methacrylic acid (MA) copolymer (polymerization ratio [mass ratio] 90:10, weight average molecular weight 85,000, glass transition temperature 80 ° C.) A separator was prepared in the same manner as in Example 1 except that the mass ratio of the polyvinylidene fluoride resin to the acrylic resin was changed as shown in Table 1.

Table 1 shows the physical properties and evaluation results of each of the separators of Examples 1 to 10 and Comparative Examples 1 to 3.

Claims (3)

Porous substrate and
An adhesive porous layer provided on one or both sides of the porous substrate and containing an acrylic resin and a polyvinylidene fluoride resin is provided.
The adhesive porous layer has a porous structure in which the acrylic resin and the polyvinylidene fluoride-based resin are mixed.
In the adhesive porous layer, the acrylic resin is contained in an amount of 2 to 40% by mass with respect to the total mass of the acrylic resin and the polyvinylidene fluoride-based resin.
The acrylic resin has two types of acrylic monomers selected from the group consisting of 2-hydroxyethyl methacrylate, ethyl acrylate, butyl acrylate, methyl methacrylate, and polymethoxydiethylene glycol (meth) acrylate as monomer components. And a separator for non-aqueous secondary batteries, which is a ternary copolymer containing a styrene monomer. The polyvinylidene fluoride-based resin is a copolymer containing vinylidene fluoride and hexafluoropropylene as monomer components, and the content of the hexafluoropropylene monomer component in the copolymer is 3% by mass to 20% by mass. The separator for a non-aqueous secondary battery according to claim 1, wherein the weight average molecular weight of the copolymer is 100,000 to 1,500,000. A non-aqueous secondary battery separator according to claim 1 or 2, which is provided between a positive electrode, a negative electrode, and the positive electrode and the negative electrode, and obtains an electromotive force by doping / dedoping lithium. Water-based secondary battery.