JP2509768B2 - Multilayer stack - Google Patents

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a multilayer laminate, and more particularly to a multilayer laminate excellent in gas barrier performance, mechanical strength and the like.

[0002]

Conventionally, as a multilayer laminate having gas barrier performance, a polyamide resin, a polyvinylidene chloride copolymer resin, an olefin-vinyl acetate copolymer saponified product (in particular, an ethylene-vinyl acetate copolymer saponified product). It is known to use a resin having a high gas barrier property such as. Among them, the saponified ethylene-vinyl acetate copolymer (hereinafter sometimes abbreviated as EVOH) has the most excellent gas barrier property and fragrance-preserving property of aroma components, and therefore, in various packaging fields, films, sheets, It is used as a container for bottles, pouches, tubes, etc. However, EVOH is not used alone because of problems such as heat sealability and deterioration of gas barrier property due to moisture absorption, but it is often used by being laminated with another thermoplastic resin. Among these other thermoplastic resins, a polyester resin [especially polyethylene terephthalate (hereinafter sometimes abbreviated as PET)] has excellent mechanical strength, heat resistance, and weather resistance, and therefore, the film Widely used as molded products such as bottles. However, PET has a poor gas barrier property and has a problem that the content to be filled in a PET molded product is limited. In order to solve this problem, a method of stacking EVOH on PET has been considered. However, PET and EVOH have a poor affinity,
When laminated in multiple layers, an adhesive layer is required between the PET and EVOH layers. Moreover, a product such as a stretched bottle is often subjected to a large deformation such as a stretching process after being laminated.

As a method for improving the interlaminar adhesiveness, for example, as described in JP-A-51-98784, unsaturated carboxylic acid or its anhydride component is 0.0.
The modified polyolefin, which is 1 to 10% by weight, is added with 60 to 95% by weight, and 40 parts of the rubber part having a Mooney viscosity of 40 to 150 is added.
To 5 wt%, or a polyester resin composition containing a polyalkylene glycol described in JP-A-60-13547 or a glycol mainly containing the polyalkylene glycol,
Resin mixture with α-olefin / maleic anhydride copolymer, polymer having amide repeating unit described in JP-A-60-193648 and oxysilane ring-containing compound and acid or acid anhydride group-containing compound and / or amino A composition containing a compound, a polymer having an ester repeating unit described in JP-A-60-139772, an oxysilane ring-containing compound, and an acid or acid anhydride group-containing compound,
JP-A-64-20134 and JP-A-64-20
The ratio of ester group / amide group described in Japanese Patent Publication No. 135
90/10 to 10/90 (molar ratio) polyester-amide adhesive resin, a method of blending a polyamide-ester thermoplastic resin in an EVOH layer as described in JP-A-1-176554, or RECYCL
E'89 P-207 DAVOS / SWITZERLAND, 1989.4.10-
4.13 (MAACK BUSINESS SERVICES) as described in ethylene-ethyl acrylate-glycidyl maleate terpolymer resin and Convertec November 1987 P-3
As described in 6, an ethylene-ethyl acrylate-maleic anhydride terpolymer resin and the like are known.

Each of these conventional methods has a problem that the interlayer adhesion strength is poor and peeling is easy. As described above, there is no one in which PET and EVOH or the like are firmly adhered and laminated, and therefore, the multilayer container in which the synthetic resin layer is fixed so as to cover the gas barrier layer at the end where the cross section of the multilayer plate is exposed (special feature: KAISHO 63-125141) is known. Even in this method, since the body of the container is not adhered at all, it is easily peeled off when stress is applied such as gripping or dropping, and when it is remarkable, pinholes are generated in the gas barrier layer, and the gas barrier property is extremely high. There are problems such as deterioration.

By the way, generally, a polyvinyl alcohol resin (hereinafter sometimes abbreviated as PVA) has a melting temperature and a thermal decomposition temperature extremely close to each other, and thus melt extrusion cannot be performed. Further, although the PVA film is flexible and tough under high humidity, there is a problem that it loses flexibility and becomes brittle and easily broken under low humidity. As a solution to this problem, a method has been known in which an α-olefin and vinyl acetate are copolymerized and saponified.
Since PVA cannot be melt-extruded, for example, as a method for obtaining a film, as disclosed in Poval P-374: Polymer Publishing Association (published April 25, 1984), PVA was mixed with water and glycosyl chloride. -Casting method in which it is melted with a plasticizer such as resin and cast on a drying drum or belt through a slit, or is applied by a roll coater, and moisture is dried on the drum or belt to obtain a film, and PVA. A method is known in which a plasticizer and an appropriate amount of water are impregnated to form pellets, and extrusion is performed using an extruder having a special melting, kneading and defoaming mechanism. This extrusion method is based on BRITISH POLYMER JOURNAL VOL.20, NO.4, P335 (1
988), the PVA solution is continuously formed by a twin-screw extruder, and the aqueous solution is introduced into a single-screw extruder, pressure-measured while uniformizing the temperature, filtered, and then extruded from a T-die. . As described above, the molding of PVA requires a special molding machine, requires a filtration step for removing the gel component and a step of drying the water content of the aqueous solution after the film formation, and is very complicated. Therefore, it has been desired that the resin can be easily melt-molded like a thermoplastic resin.

As a method for making PVA melt-moldable and preventing weakening, for example, dipropylene glycol,
It is known that a plasticizer such as triethylene glycol, diethylene glycol or glycerin is added to PVA to lower the melting point or the flow starting temperature. This method is described in detail in RKTubbs, J. Polymer. Sci, A3, 4181 (1965) and Polymer Chemistry Vol. 26, P118 (1969). However, although this method is effective in lowering the flow initiation temperature, it lowers the gas barrier property or generally lowers the strength, and tends to absorb moisture at high temperatures and soften. On the other hand, it tends to become hard and brittle at low temperatures. Further, there is a problem that the plasticizer bleeds on the surface of the molded product when stored for a long time.

Further, a method in which EVOH is mixed with PVA to enable melt molding (JP-A-49-33945), a saponification product of a long-chain α-olefin-vinyl acetate copolymer having 5 to 30 carbon atoms ( Modified PVA) and a polymer excluding polyolefin (JP-A-49-117536), a method of mixing EVOH with PVA to enable melt molding (JP-A-49-33945), a modified PVA. Method of mixing bisphenols (JP-A-50-123)
151), a method in which a polyolefin resin is grafted to PVA, and the grafted product is mixed with PVA and the polyolefin resin to enable melt molding (JP-A-60-188).
No. 488) is known. However, all of these methods are inferior in melt moldability, have no interlayer adhesion between polyester resin such as PET and EVOH, and are difficult to use as an adhesive resin between PET and EVOH.
Even if it is directly laminated on ET, the PVA film cracks, a gas barrier property is not obtained, and the PVA film is easily peeled off.

[0008]

SUMMARY OF THE INVENTION An object of the present invention is to obtain a multi-layer laminate having no delamination, excellent long-term storage stability, gas barrier performance and mechanical strength.

[0009]

That is, the present invention is
(A) An ethylene content of 1 to 50 wt% obtained by emulsion polymerization of a vinyl acetate monomer and an ethylene monomer in a state where polyvinyl alcohol is present in an amount of 3% by weight or more and less than 10% by weight based on the total amount of polyvinyl alcohol and vinyl acetate monomer % Polyvinyl alcohol-based copolymer resin 5 to 95% by weight and (B) polyvinyl alcohol-based resin 95 to 5% by weight, a multilayer laminate formed by laminating a polyvinyl alcohol-based resin composition layer and a polyester resin layer. It is provided. In the multilayer laminate of the present invention, when directly laminated on a polyester resin layer such as PET, by using a resin composition comprising (A) a polyvinyl alcohol-based copolymer resin and (B) a polyvinyl alcohol-based resin, Does not require a special adhesive layer,
Moreover, it is possible to obtain a multilayer laminate having excellent gas barrier performance. That is, since it has both the adhesive function and the gas barrier function, the number of laminated layers can be smaller than that of the conventional multilayer laminated body, which is economical.

Regarding the polyvinyl alcohol copolymer resin which is the component (A) in the polyvinyl alcohol resin composition layer constituting the present invention, for example, JP-A-60-9 is used.
It can be produced by the method described in Japanese Patent No. 6637 and Japanese Patent Laid-Open No. 63-108016.
One example of the method for producing the polyvinyl alcohol-based copolymer resin is to copolymerize with a vinyl acetate monomer and an ethylene monomer using a known catalyst in the presence of polyvinyl alcohol having an average degree of polymerization of 20 to 5,000. Is obtained by The polyvinyl alcohol used in this case may have an arbitrary degree of hydrolysis, but preferably has an average saponification degree of 50 to 99%, particularly 70 to 99%.
Are more preferred. Especially, the average saponification degree is 70 to 9
It is preferable that the average degree of polymerization is 9% and the average degree of polymerization is 100 to 3,000, and the average degree of saponification is 78 to 99% and the average degree of polymerization is 300 to 300.
2,500 is the best. During the copolymerization reaction of the vinyl acetate monomer and the ethylene monomer, the amount of polyvinyl alcohol present in the aqueous emulsion must be 3% by weight or more and less than 10% by weight based on the total amount of the vinyl acetate monomer and polyvinyl alcohol. If it is less than 3% by weight, the compatibility with the polyvinyl alcohol-based resin is poor and it is not suitable for the purpose of the present invention. On the other hand, when it is present in an amount of 10% by weight or more, the resin composition with the component (B) tends to be slightly hardened, which may not be preferable depending on the purpose of use.

The content of ethylene in the polyvinyl alcohol-based copolymer produced by the above method is 1 to 50% by weight, preferably 10 to 45% by weight. When the ethylene content exceeds 50% by weight, the compatibility with PVA is poor and it is not suitable for the purpose of the present invention. On the other hand, if it is less than 1% by weight, it cannot be used because of poor melt moldability. The content of vinyl acetate unit is not particularly limited, but 1
~ 89% by weight is preferred. If it is less than 1% by weight, the melt moldability will be poor, and if it exceeds 89% by weight, the gas barrier performance will be poor. In this polyvinyl alcohol-based copolymer resin, the following monomers may be copolymerized in place of the ethylene monomer, or a vinyl acetate monomer and an ethylene monomer may be further copolymerized with a monomer having an ethylenic unsaturated bond. I can. Examples of these monomers include
Unsaturated acids such as acrylic acid, methacrylic acid, crotonic acid, maleic acid, fumaric acid, itaconic acid or their alkyl esters, acrylamide, methacrylamide, unsaturated carboxylic acid amides such as N-methylolacrylamide, styrene, acrylonitrile or acrylic Functional group monomers such as 2-hydroxyethyl acid ester, 2-hydroxyethyl methacrylate, glycidyl methacrylate, and α-olefins such as propylene, butene, decene and octadecene, vinyl propionate, vinyl pivalate, vinyl laurate, versatic Examples thereof include vinyl esters such as vinyl acetate, vinyl chloride, vinyl fluoride and the like.

On the other hand, the polyvinyl alcohol resin (PVA), which is the component (B) in the polyvinyl alcohol resin composition layer constituting the present invention, means a partially or completely saponified product of polyvinyl acetate or its modified polyvinyl. Refers to alcohol resin. Polymerization methods for polyvinyl acetate include bulk polymerization, solution polymerization, emulsion polymerization, and suspension polymerization. Of these, bulk polymerization has problems such as increase in viscosity during polymerization, adhesion of polymer to a polymerization vessel, and difficulty in removing heat of polymerization.
Not preferred. On the other hand, in emulsion polymerization, the emulsion-polymerized liquid is used as it is as a raw material for adhesives and paints.
It is not often used as a method for producing polyvinyl acetate. In addition, suspension polymerization has a problem that it is difficult to control production conditions and the like. Therefore, the solution polymerization described below is generally used as a method for producing polyvinyl acetate. This solution polymerization employs a method in which a vinyl acetate monomer is diluted with a solvent such as methanol, ethanol, or methyl acetate, a catalyst is added to carry out polymerization, and the heat of polymerization is removed by the heat of evaporation of the solvent. Since solution polymerization has a low viscosity, stirring is facilitated and removal of heat of polymerization is facilitated. These polymerizations are usually carried out by a method using a thermal decomposition initiator. Here, benzoyl peroxide (BPO), azobisisobutyronitrile (AIBN) or the like is usually used as an initiator that decomposes by heat. In addition, polymerization by ultraviolet rays, polymerization by radiation such as gamma rays, Redox
There is catalytic low temperature polymerization. However, these methods have not yet been used on an industrial scale. By subjecting the thus-polymerized polyvinyl acetate to a saponification reaction using an alkali catalyst or an acid catalyst, a polyvinyl alcohol resin (PVA) which is the component (B) of the present invention can be obtained.

The modified polyvinyl alcohol resin is a partially or completely saponified product of the copolymer described below. For example, a copolymer of vinyl acetate and an olefin having 4 to 18 carbon atoms, a copolymer of vinyl acetate and vinyl carboxylate (vinyl versatate, vinyl stearate, etc.), vinyl acetate and alkyl vinyl ether (lauryl vinyl ether, methyl). Copolymers with vinyl ether, etc., copolymers with vinyl acetate and (meth) acrylate (methyl methacrylate), vinyl acetate and acrylamide (acrylamide; methacrylamide; N, N-dimethylacrylamide, etc.) Copolymers of vinyl acetate and unsaturated carboxylic acids or their anhydrides or esters (acrylic acid, crotonic acid, maleic acid, fumaric acid,
Copolymers with itaconic acid, etc., copolymers with vinyl acetate and sulfonic acid monomers (vinyl sulfonic acid, acrysulfonic acid, etc.), vinyl acetate and cationic monomers (dimethylaminoethyl methacrylate, vinyl imidazole,
Vinyl pyridine, vinyl succinimide, etc.), copolymers of vinyl acetate and other monomers (vinylene carbonate, allyl alcohol, allyl acetate, etc.).

The polyvinyl alcohol resin (PVA) thus obtained is composed of vinyl alcohol units and vinyl acetate units, and the degree of polymerization thereof is not particularly limited and may be appropriately selected according to the application. However, it is usually 50 to 2,500. Above all, a polymer having a degree of polymerization of 200 to 1,800 is preferable in view of melt fluidity and mechanical strength. On the other hand, the degree of saponification is 50 mol%
The above is good, and in view of gas barrier performance and melt fluidity, a saponification degree of 70 to 99.5 mol% is preferable. If the saponification degree is less than 50 mol%, the mechanical strength is poor, while if it exceeds 99.5 mol%, the melt fluidity is poor.

In the polyvinyl alcohol resin composition layer used in the present invention, the mixing ratio of the polyvinyl alcohol copolymer resin as the component (A) and the polyvinyl alcohol resin (PVA) as the component (B) is polyvinyl alcohol. Copolymer resin 5 to 95% by weight, PVA 95 to
5% by weight, preferably 15 to 85% by weight of polyvinyl alcohol copolymer resin, 85 to 15% by weight of PVA
Is. This is because when the polyvinyl alcohol copolymer resin is less than 5% by weight, the adhesive performance with a polyester resin such as PET is impaired, which is not preferable. On the other hand, if it exceeds 95% by weight, the gas barrier property is deteriorated, which is not preferable. When used as an adhesive resin, the polyvinyl alcohol resin composition layer has a melting index (MFR, JIS-K675).
The load of 2.16 kg and the temperature of 230 ° C. is not particularly limited and may be appropriately selected according to the molding method, but in the case of extrusion molding, the range of 0.1 to 50 g / 10 minutes is appropriate. is there.

As a result of further studies on the problem of a PET multilayer laminate, the present inventors have found that a polyvinyl alcohol resin composition comprising components (A) and (B) is
When used as an adhesive layer of a polyester resin typified by 1) and an olefin-vinyl acetate copolymer saponified resin typified by EVOH, this resin composition has both the function of the adhesive layer and the function of gas barrier property. It has been found that a multi-layer laminate that is economical, has excellent interlayer adhesive strength, and has excellent gas barrier properties can be obtained.

Here, the polyester resin constituting the present invention includes terephthalic acid, phthalic acid, isophthalic acid;
-Naphthalene dicarboxylic acid; 1,5-naphthalene dicarboxylic acid, aromatic dicarboxylic acid such as methyl terephthalic acid,
Aliphatic dicarboxylic acids such as sebacic acid, adipic acid, azelaic acid and succinic acid, dicarboxylic acids such as alicyclic dicarboxylic acids such as hexahydroterephthalic acid and hexahydroisophthalic acid, and ester-forming derivatives thereof, for example, lower alkyl esters , Acid anhydrides and the like, ethylene glycol, propylene glycol, tetramethylene glycol, pentamethylene glycol, hexamethylene glycol; aliphatic alkylene glycols such as 1,7-heptanediol, neopentyl glycol, diethylene glycol, triethylene glycol, tetraethylene glycol , Alkylene oxide glycols such as dipropylene glycol and dibutylene glycol, glycols such as alicyclic glycols such as 1,4-cyclohexanemethanol and ester forms thereof It is synthesized from the sex derivatives.

The saponified olefin-vinyl acetate copolymer resin is a partial or complete saponification product of a copolymer of various olefins, for example, olefins such as ethylene, propylene and butene-1 and vinyl acetate. For example, there are saponified products of ethylene-vinyl acetate copolymer and saponified products of propylene-vinyl acetate copolymer. Particularly, because of easy polymerization, saponified ethylene-vinyl acetate copolymer (EVO
H) is preferred. There are various EVOHs, and those having a composition with an ethylene content of 15 to 60 mol% and a saponification degree of 90 mol% or more are preferably used. When the ethylene content is less than 15 mol%, the melt moldability is deteriorated,
Further, if the degree of saponification of the vinyl acetate component is less than 90 mol%, the gas barrier property may deteriorate. Particularly preferred is EVOH having an ethylene content of 25 to 50 mol% and a saponification degree of 96 mol% or more. In addition to ethylene and vinyl acetate (or vinyl alcohol obtained by saponifying it), unsaturated acids such as acrylic acid, methacrylic acid, crotonic acid, maleic acid or alkyl esters thereof, propylene, butene, α-decene, α-α such as octadecene
-A small amount of olefin etc. may be contained as a comonomer.

The multilayer laminate of the present invention can be formed into a film, a sheet, a tube, a bottle, etc. by a known melt molding method and coating method. For example, as such a laminating method, a co-extrusion molding method (feed block, multi-manifold method) co-injection molding method, co-extrusion pipe molding method, and a resin composition comprising a polyvinyl alcohol-based copolymer resin and a polyvinyl alcohol-based resin There are various methods such as a coating molding method in which is coated with a doctor knife or a coater equipped with a gravure roll. The multilayer laminate thus obtained is further reheated by using a vacuum forming machine, a pressure forming machine, a stretch blow molding machine or the like, and a stretching operation is applied, or the above-mentioned multilayer laminate is uniaxially or biaxially stretched. A heat stretching operation can be performed using a machine. And as a laminated form, polyester resin layer / polyvinyl alcohol resin composition layer / polyester resin layer, polyester resin layer / polyvinyl alcohol resin composition layer / olefin-vinyl acetate copolymer saponified resin layer, polyester resin layer / Polyvinyl alcohol resin composition layer / polyethylene resin layer, polyester resin layer / polyvinyl alcohol resin composition layer / polypropylene resin layer, polyester resin layer / polyvinyl alcohol resin composition layer / polystyrene resin layer, etc. You can

If desired, the following other thermoplastic resins may be laminated on the multilayer laminate of the present invention. Other thermoplastic resins include polyethylene resins, polypropylene resins, copolymers of ethylene and α-olefins having 3 to 12 carbon atoms, polyolefin resins such as ionomer resins, polystyrene resins, polyvinyl chloride resins, polycarbonate resins, polyamides. There are thermoplastic resins such as resins. Here, the copolymer of ethylene and an α-olefin having 3 to 12 carbon atoms means an ethylene-butene-1 copolymer, an ethylene-4 methylpentene-1 copolymer, an ethylene-hexene-1 copolymer. And modified polypropylene blended with ethylene-propylene rubber, modified polybutene, modified poly-4 methylpentene, or the above-mentioned polyolefin polymer with an unsaturated carboxylic acid or its anhydride grafted with an organic peroxide or Those copolymerized with other monomers (eg, methyl methacrylate, ethyl acrylate, etc.) are also included in the object.

[0021]

When a resin composition prepared by blending a polyvinyl alcohol-based copolymer resin (A) with a polyvinyl alcohol-based resin (B) which cannot be melt-extruded is laminated on a polyester resin, or a polyester resin and an olefin-vinyl acetate saponified product When laminated as an adhesive layer with a resin, the cause of excellent gas barrier performance, mechanical strength, and excellent interlaminar adhesion strength between the two is not clear, but mixing of both causes some interaction with the polyester resin and is effective. It seems that it can be bonded to.

[0022]

EXAMPLES The present invention will be described in more detail with reference to Examples and Comparative Examples. Examples 1 to 4 and Comparative Examples 1 and 2 (Preparation of Polyvinyl Alcohol Copolymer Resin) An autoclave having an inner volume of 30 liters was used, and the degree of polymerization was 50.
0, a partially saponified polyvinyl alcohol resin PVA205 manufactured by Kuraray Co., Ltd. having a saponification degree of 88% was used, while adding the catalyst ammonium persulfate and sodium metabisulfite, and changing the vinyl acetate concentration and the ethylene gas pressure. Emulsion polymerization was carried out to obtain a polyvinyl alcohol copolymer resin having the composition shown in Table 1. The solid content concentration of the polymerized emulsion was about 20 to 60% by weight.

[0023]

[Table 1]

(Drying of emulsion) This emulsion was left standing at -20 ° C for 20 hours to freeze-precipitate to obtain a polymer. The resulting polymer is then freeze-milled, freeze-dried,
It was vacuum dried at a temperature of 80 ° C. The ratio of the ethylene component of the polymer was determined by the alkali saponification method.

(Mixing of polyvinyl alcohol copolymer resin and polyvinyl alcohol resin) Kobe Steel KT
Using an X twin-screw extruder, the polyvinyl alcohol-based copolymer resin and the polyvinyl alcohol-based resin were mixed at a temperature of 220 ° C. to obtain a resin composition shown in Table 2.

[0026]

[Table 2]

(Preparation of Multilayer Laminate) The resin composition thus obtained was processed by PE using a multilayer cast film molding machine.
A film having a thickness of 20/20/20 μm was obtained with a T / resin composition / PET two-kind three-layer structure. In addition, PET
The resin used had a concentration of 0.5 g per 100 ml of the orthochlorophenol solution and a relative viscosity of 0.7 at 25 ° C.

Examples 5 to 7 PET / resin composition / EVO was prepared by using Soarnol DT manufactured by Nippon Synthetic Chemical Industry Co., Ltd., which is EVOH having an ethylene content of about 29 mol%, and using the resin compositions shown in Table 2.
A film having a thickness of 20/20/20 μm was obtained with a three-layer three-layer structure of H. Comparative Examples 3 and 4 As an adhesive resin layer, LOTAD manufactured by NORSOLOR, which is an ethylene-ethyl acrylate-glycidyl methacrylate terpolymer resin instead of the above resin composition.
Comparative Example 3 was performed in the same manner as in the above-mentioned example except that ER AX8660 was used. In addition, an ethylene-vinyl acetate copolymer saponified resin having a vinyl acetate content of 10% by weight, which was melt-graft modified with maleic anhydride by about 1.6% by weight using an extruder, was used as an adhesive resin layer. Comparative Example 4 was used.

(Evaluation of Interlaminar Adhesive Strength and Oxygen Gas Barrier Property) As a performance evaluation of the multilayer laminates obtained in Examples and Comparative Examples, the interlaminar adhesive strength was measured using a tensile tester manufactured by Toyo Seiki Co., Ltd., a peeling speed of 300 mm / min. It was measured at. Further, the oxygen transmission rate was measured using OXTRAN-10 / 50A manufactured by Modern Control Co., Ltd. for the above film. Tables 3 and 4 show the results of measuring the interlayer adhesive strength and the amount of oxygen permeation of the multilayer laminates obtained in each example and comparative example.

[0030]

[Table 3]

[0031]

[Table 4]

[0032]

As described above, the multilayer laminate of the present invention can be obtained by a melt molding method, a coating method or the like, and is excellent in interlayer adhesion strength and gas barrier property. Therefore, the multilayer laminate of the present invention can be effectively used for food packaging materials, pharmaceutical packaging materials, cosmetic packaging materials, containers for which gas barrier properties are required, and the like.

Front page continuation (72) Inventor Akio Harada 1-251-1, Ibochu, Ibocho-cho, Tatsuno-shi, Hyogo Showa Polymer Co., Ltd. Osaka Research Institute (72) 1-251-1 Ibanaka, Ibocho, Tatsuno-shi, Hyogo Prefecture (56) Reference JP-A-3-161334 (JP, A) JP-A-2-182451 (JP, A)

Claims (5)

(57) [Claims] 1. An ethylene-containing product obtained by emulsion-polymerizing a vinyl acetate monomer and an ethylene monomer, wherein (A) polyvinyl alcohol is present in an amount of 3% by weight or more and less than 10% by weight based on the total amount of polyvinyl alcohol and vinyl acetate monomer. An amount of 1 to 50% by weight of a polyvinyl alcohol copolymer resin and a (B) polyvinyl alcohol resin of 95 to 5% by weight, and a polyvinyl alcohol resin composition layer and a polyester resin layer are laminated. Multi-layered laminate. 2. The multilayer laminate according to claim 1, which has a layer structure of polyester resin layer / polyvinyl alcohol resin composition layer / polyester resin layer. 3. A multilayer laminate containing a polyester resin layer and an olefin-vinyl acetate copolymer saponified resin layer, wherein the adhesive layer is the polyvinyl alcohol resin composition layer of claim 1. 4. The polyvinyl alcohol resin as the component (B) comprises a vinyl alcohol unit and a vinyl acetate unit, and has a polymerization degree of 50 to 2,500 and a saponification degree of 50 mol% or more. The multilayer laminate according to claim 1. 5. The multilayer laminate according to claim 3, wherein the saponified olefin-vinyl acetate copolymer resin has an ethylene unit content of 15 to 60 mol% and a saponification degree of 90 mol% or more.