WO2007129371A1 - 多層フィルム - Google Patents
多層フィルム Download PDFInfo
- Publication number
- WO2007129371A1 WO2007129371A1 PCT/JP2006/308673 JP2006308673W WO2007129371A1 WO 2007129371 A1 WO2007129371 A1 WO 2007129371A1 JP 2006308673 W JP2006308673 W JP 2006308673W WO 2007129371 A1 WO2007129371 A1 WO 2007129371A1
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- WIPO (PCT)
- Prior art keywords
- multilayer film
- ethylene
- evoh
- structural unit
- alcohol copolymer
- Prior art date
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/30—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers
- B32B27/306—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers comprising vinyl acetate or vinyl alcohol (co)polymers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/12—Making granules characterised by structure or composition
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
- B32B27/08—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B7/00—Layered products characterised by the relation between layers; Layered products characterised by the relative orientation of features between layers, or by the relative values of a measurable parameter between layers, i.e. products comprising layers having different physical, chemical or physicochemical properties; Layered products characterised by the interconnection of layers
- B32B7/04—Interconnection of layers
- B32B7/12—Interconnection of layers using interposed adhesives or interposed materials with bonding properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/02—Making granules by dividing preformed material
- B29B9/06—Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/40—Properties of the layers or laminate having particular optical properties
- B32B2307/412—Transparent
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2439/00—Containers; Receptacles
- B32B2439/70—Food packaging
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2439/00—Containers; Receptacles
- B32B2439/80—Medical packaging
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/26—Web or sheet containing structurally defined element or component, the element or component having a specified physical dimension
- Y10T428/269—Web or sheet containing structurally defined element or component, the element or component having a specified physical dimension including synthetic resin or polymer layer or component
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31855—Of addition polymer from unsaturated monomers
- Y10T428/31909—Next to second addition polymer from unsaturated monomers
- Y10T428/31913—Monoolefin polymer
Definitions
- the present invention relates to a multilayer film of an ethylene vinyl alcohol copolymer (hereinafter abbreviated as EVOH) and a thermoplastic resin, and more specifically, adhesion, appearance, flex resistance, stretchability, and gas noriality And a multilayer stretched film obtained by stretching a strong multilayer film.
- EVOH ethylene vinyl alcohol copolymer
- thermoplastic resin thermoplastic resin
- EVOH is excellent in transparency, gas noria, aroma retention, solvent resistance, oil resistance, etc., and has been used for food packaging materials, pharmaceutical packaging materials, industrial chemical packaging materials. It is used after being formed into films and sheets of agricultural chemical packaging materials, or containers such as tubes, cups, trays, and bottles.
- thermoplastic resin In general, it is often used as a multilayer film laminated with other thermoplastic resin for the purpose of supplementing the mechanical properties and moisture resistance of EVOH. Laminated with rosin and used. However, polyolefin resin and EVOH have no adhesive strength! Therefore, they are used by laminating an adhesive resin layer such as unsaturated carboxylic acid modified polyolefin resin between the polyolefin resin layer and EVOH layer.
- a strong multilayer film may be subjected to stretching treatment for the purpose of improving the physical properties of other thermoplastic resins and the barrier performance of EVOH.
- Patent Document 1 Japanese Patent Laid-Open No. 01-135852
- Patent Document 2 Japanese Patent Laid-Open No. 10-067898
- Patent Document 3 Japanese Patent Laid-Open No. 07-108655
- Patent Document 4 Japanese Patent Laid-Open No. 53--088067
- Patent Document 5 Japanese Patent Laid-Open No. 59- — 020345
- Patent Document 6 JP-A 52- — 141785
- Patent Document 7 Japanese Patent Laid-Open No. 58- — 036412
- Patent Document 8 Japanese Patent Laid-Open No. 63-125125
- Patent Document 9 Japanese Unexamined Patent Publication No. 63--179935
- Patent Document 10 Japanese Patent Application Laid-Open No. 08-311276
- Patent Document 11 Japanese Patent Laid-Open No. 2000-336230
- the gas barrier property is insufficient when the method 4) is used, and the stretch between EVOH and other resins is poor when the method 5) is stretched.
- the gas noreality may be reduced, or the transparency of the film may be reduced.
- the gas noriality may be lowered when stretched at a high magnification. It became clear that pinholes were generated by force and repeated bending due to the decrease in flexibility, and gas noliaability decreased. [0007] Therefore, a multilayer film having good adhesiveness and excellent appearance, bending resistance, stretchability, gas barrier properties, and bending resistance, and a multilayer stretched film obtained by stretching a strong multilayer film are provided. This is what is desired. Means for solving the problem
- Multi-layer film made by laminating a thermoplastic resin-containing layer on one or both sides of a VOH-containing layer
- the inventors have found that a multilayer stretched film obtained by stretching a strong multilayer film meets the above-mentioned purpose, and has completed the present invention.
- X is a bonding chain and is an arbitrary bonding chain excluding an ether bond
- R1 to R4 are each independently an arbitrary substituent
- n represents 0 or 1.
- the thermoplastic resin is a polyolefin-based thermoplastic resin, laminated via an adhesive resin, and 0.1 to 30 mol of the structural unit (1).
- the preferred embodiment is a multilayer film formed by laminating a thermoplastic resin with EVOH containing 0.001 to 1 part by weight of a boron compound in terms of boron with respect to 100 parts of EVOH. .
- the multilayer film of the present invention has a layer of EVOH containing a specific structural unit. Therefore, it has excellent adhesion, appearance, transparency, bending resistance, stretchability, gas barrier properties, and bending resistance even during high-speed film formation.
- FIG. 1 is a 1 H-NMR chart before saponification of EVOH obtained in Polymerization Example 1.
- FIG. 2 is a 1 H-NMR chart of EVOH obtained in Polymerization Example 1.
- EVOH used for the multilayer film of the present invention is EVOH characterized in that it contains the above structural unit (1), that is, a structural unit having a 1,2-glycol bond in the side chain.
- 2-Glycol bond structure (X) linking to the bond structure can be applied to any bond chain except for ether bond, and the bond chain is not particularly limited, but alkylene, alkene-
- hydrocarbons such as phenylene and naphthylene (these hydrocarbons may be substituted with halogens such as fluorine, chlorine and bromine), as well as —CO— and —COCO— , —CO (CH) CO—, —CO (CH) CO
- R —, —OAl (OR) —, —OAl (OR) 0—, etc.
- R is independently an arbitrary substituent, and a hydrogen atom or an alkyl group is preferred
- the ether bond is not preferable in that it decomposes during melt molding and decreases the thermal melting stability of EVOH.
- alkylene is preferred as the bond type from the viewpoint of heat melting stability, and alkylene having 6 or less carbon atoms is preferred.
- EVOH has a favorable gas barrier performance, and a carbon atom having a smaller number of carbon atoms is preferred.
- R1 to R4 are arbitrary substituents, and although not particularly limited, hydrogen atoms and alkyl groups are preferred in terms of easy availability of monomers, and hydrogen atoms have good gas barrier properties of EVOH. This is preferable.
- the EVOH production method described above is not particularly limited, but when a structural unit in which a 1,2 glycol bond structure is directly bonded to the main chain, which is the most preferable structure, is taken as an example, 3, 4 diol 1-butene, butyl A method of saponifying a copolymer obtained by copolymerizing an ester monomer and ethylene, and a copolymer obtained by copolymerizing a 3, 4 dihydroxy 1-butene, a butyl ester monomer and ethylene.
- those having alkylene as the connecting chain (X) include 4,5-diol 1-pentene, 4,5-dioxy 1-pentene, 4,5-diol 3-methyl-1-pentene, 4,5 diol 3— Examples include a method in which a copolymer obtained by copolymerizing methyl-1 pentene, 5, 6 diol 1 hexene, 5, 6 disiloxy 1 hexene, etc., a vinyl ester monomer and ethylene is used.
- R is an alkyl group, preferably a methyl group.
- R is an alkyl group, preferably a methyl group.
- R is an alkyl group, preferably a methyl group.
- the compound represented by the above formula (2) can be obtained from Eastman Chemical Co., and the compound represented by the above formula (3) can be obtained from Eastman Chemical Co., Ltd.
- bull ester monomer formic acid, acetic acid, propionic acid, valeric acid, butyric acid, butyric acid, isobutyric acid, pivalate, power purate, lauric acid, stearic acid, Powers including benzoic acid burs, versatic acid bulls, etc.
- vinyl acetate is preferably used from an economical viewpoint.
- the method for charging the monomer component at the time of copolymerization is not particularly limited, and any method such as batch charging, split charging, or continuous charging may be employed.
- normal ethylene pressure polymerization may be carried out, and the amount introduced can be controlled by the pressure of ethylene. Is usually selected from the range of 25-80 kg / cm 2 .
- Examples of the solvent used in intensive copolymerization usually include lower alcohols such as methanol, ethanol, propanol and butanol, and ketones such as acetone and methyl ethyl ketone. Are preferably used.
- a polymerization catalyst is used for the copolymerization.
- a strong polymerization catalyst include known radical polymerization catalysts such as azobisisobutyl-tolyl, peroxide acetyl, benzoyl peroxide, and lauryl peroxide, and t-butyl peroxide.
- the reaction temperature of the copolymerization reaction is preferably selected from the range of 40 ° C to the boiling point depending on the solvent and pressure used.
- a hydroxylatatatone compound or a hydroxycarboxylic acid coexist with the above catalyst.
- the hydroxylatatatone compound may be any compound having a lactone ring and a hydroxyl group in the molecule.
- L-ascorbic acid Erythorbic acid, dalcono delta rataton, and the like.
- L-ascorbic acid and erythorbic acid are preferably used.
- Hydroxycarboxylic acids include glycolic acid, lactic acid, glyceric acid, malic acid, Examples thereof include tartaric acid, citrate, salicylic acid and the like, and preferably citrate is used.
- the amount of the hydroxylatatotone compound or hydroxycarboxylic acid used is 0.0001 to 0.1 parts by weight (moreover, 100 parts by weight of vinyl acetate in both batch and continuous types) 0. 0005-0.05 parts by weight, especially 0.001-0.03 parts by weight) Power ⁇
- the amount used is less than 0.0001 parts by weight, the coexistence effect may not be sufficiently obtained.
- it exceeds 0.1 parts by weight the polymerization of vinyl acetate is inhibited, which is not preferable.
- a powerful compound into the polymerization system it is usually diluted with a solvent such as an aliphatic ester containing low-grade aliphatic alcohol or vinyl acetate, water, or a mixed solvent thereof to the polymerization reaction system.
- a solvent such as an aliphatic ester containing low-grade aliphatic alcohol or vinyl acetate, water, or a mixed solvent thereof to the polymerization reaction system.
- the copolymerization ratio of 3,4-dihydroxy-1-butene or the like is not particularly limited, but the copolymerization ratio may be determined in accordance with the introduction amount of the structural unit (1) described above.
- a monomer that can be copolymerized with an ethylenically unsaturated monomer that can be copolymerized within a range that does not impair the effects of the present invention during the above copolymerization are olefins such as propylene, 1-butene and isobutene, unsaturated acids such as acrylic acid, methacrylic acid, crotonic acid, (anhydrous) phthalic acid, (anhydrous) maleic acid and (anhydrous) itaconic acid, or salts thereof.
- mono- or dialkyl esters having 1 to 18 carbon atoms acrylamide, N-alkyl acrylamides having 1 to 18 carbon atoms, N, N-dimethylacrylamide, 2-acrylamidopropane sulfonic acid or salts thereof, and acrylamidopropyldimethylamine.
- acrylamide such as its acid salt or its quaternary salt, methacrylamide, N-alkyl methacrylamide having 1 to 18 carbon atoms, N , N-dimethylmethacrylamide, 2-methacrylamide propanesulfonic acid or its salt, methacrylamide such as methacrylamidopropyldimethylamine or its acid salt or quaternary salt, N-butyrrolidone, N-vinylformamide N-Buramides such as N-Bulacetoamide, cyanide burs such as acryl-tolyl and methacrylate-tolyl, vinyl ethers such as C1-C18 alkyl bur
- N-acrylamidomethyltrimethylammonium chloride N-acrylamidoethyltrimethylammonium chloride, N-acrylamidopropyltrimethylammonium chloride, 2-ataryloxetyltrimethylammonium chloride, 2-methacrylochichetyl Trimethylammonium chloride, 2-hydroxy-3-methacryloyloxypropyltrimethylammonium chloride, allyltrimethylammonium chloride, methallyltrimethylammonium chloride, 3-butenetrimethylammonium chloride, dimethyldiarylammo- Cationic group-containing monomers such as um chloride and jetyl diallyl ammonium chloride, and acetoacetyl group-containing monomers are also included.
- butylsilanes include butyltrimethoxysilane, butylmethyldimethoxysilane, vinyldimethylmethoxysilane, vinyltriethoxysilane, vinylmethyljetoxysilane, vinyldimethylethoxysilane, vinylisobutyldimethoxysilane, buleti vinyltributoxy.
- Silane vinyl methoxydihexyloxy silane, burdimethoxy hexyloxy silane, vinyl trihexyloxy silane, vinyl methoxy dioxy xy silane, bur di methoxy dioxy xy silane, butyl trioctyl oxy silane, bul methoxy di lauryl oxy silane, bul Examples thereof include dimethoxylauryloxysilane, butylmethoxydiole xysilane, and burdimethoxydiolate xysilane.
- the alkaline catalyst or the catalyst obtained in the state in which the copolymer obtained above is dissolved in alcohol or hydrous alcohol is used. It is carried out using an acid catalyst.
- the alcohol methanol, which includes methanol, ethanol, propanol, tert-butanol and the like, is particularly preferably used.
- concentration of the copolymer in the alcohol is appropriately selected according to the viscosity of the system, but usually a range force of 10 to 60% by weight is also selected.
- hydroxide Alkali metal hydroxides and alcoholates such as sodium, potassium hydroxide, sodium methylate, sodium ethylate, potassium methylate, lithium methylate and the like, alcoholates, sulfuric acid, hydrochloric acid, nitric acid, metasulfonic acid, Examples include acid catalysts such as zeolite and cation exchange resin.
- the amount of the strong ken-y catalyst used is appropriately selected depending on the ken-y method, the target ken-y degree, etc., but when an alkali catalyst is used, the butyl ester monomer and 3, 4 disiloxy are usually used. 0.001 to 0.1 equivalent to the total amount of 1-butene, preferably 0.005 to 0.05 equivalent force.
- the pressure at the time of can not be generally stated depending on the target ethylene content, but it is selected from the range of 2-7 kg / cm 2 , and the temperature at this time is 80-150 ° C, preferably 100-130. Selected from ° C.
- the ethylene content and saponification degree of the obtained EVOH are not particularly limited, but the ethylene content is 10 60 mole 0/0 (further 20 to 50 mole 0/0, 25 to 48 mole 0/0, especially), degree of saponification 90 mol% or more (further 95 mol% or more, particularly 99 mol% or more is suitably used ones) tend the ethylene content to be lowered Gasuno barrier property and appearance at the time of high humidity is less than 10 mole 0/0, Gasuno rear property exceeds 60 mol% in the reverse Further, if the degree of keniness is less than 90 mol%, gas barrier properties and moisture resistance tend to be lowered, which is not preferable.
- the amount of the structural unit (1) (structural unit having a 1,2 glycol bond) introduced into the obtained EVOH is not particularly limited, but is 0.1 to 30 mol% ( further 0.5 to 25 mole 0/0, especially 1 to 20 mol 0/0) Cal preferred tool force introduction amount is 0.1 mole 0/0 Not Mitsurude the effect of the present invention is sufficiently expressed On the other hand, if it exceeds 30 mol%, the gas noriality tends to decrease, which is not preferable.
- At least one of them may or may not have a structural unit having a 1,2-glycol bond! /.
- the recall bond amount can be calculated by weight average, or the ethylene content can be calculated by weight average, but to be exact, it can be calculated from the 1 H-NMR measurement results described later.
- the amount of 1,2-glycol bond can be calculated.
- EVOH having the structural unit (1) obtained by the intensive method can be used as it is, but further, acids such as acetic acid and phosphoric acid, and the like can be used without departing from the object of the present invention.
- acids such as acetic acid and phosphoric acid, and the like
- Addition of boric acid or a metal salt thereof as a metal salt of an alkali metal, alkaline earth metal, transition metal or the like, or a boron compound is preferable in terms of improving the thermal stability of the resin.
- the amount of acetic acid added should be 0.001 to 1 part by weight with 100 parts by weight of EVOH (more preferably 0.005 to 0.2 part by weight, especially 0.000 to 0.1 part by weight). If the added amount of added calories is less than 0.001 part by weight, the content may not be sufficiently obtained. Conversely, if it exceeds 1 part by weight, the appearance of the resulting molded product tends to deteriorate. This is not preferable.
- Metal borate salts include calcium borate, cobalt borate, zinc borate (such as zinc tetraborate and zinc metaborate), aluminum borate 'potassium, ammonium borate (ammonium metaborate, Ammonium tetraborate, ammonium pentaborate, ammonium octaborate, etc.), cadmium borate (cadmium orthoborate, cadmium tetraborate, etc.), potassium borate (potassium metaborate, potassium tetraborate, potassium pentaborate, Potassium hexaborate, potassium octaborate, etc.), silver borate (silver metaborate, silver tetraborate, etc.), copper borate (cupric borate, copper metaborate, copper tetraborate, etc.), boron Sodium metaborate (sodium metaborate, sodium diborate, sodium tetraborate, sodium pentaborate, sodium hexaborate, sodium
- Preferred examples include borax, boric acid, and sodium borate (sodium metaborate, sodium diborate, sodium tetraborate, sodium pentaborate, sodium hexaborate, sodium octaborate, etc.).
- the amount of boron compound added is 0.001 to 1 part by weight in terms of boron with respect to 100 parts by weight of the total EVOH in the composition (more preferably 0.002 to 0.2 parts by weight, particularly 0.005). -0.1 parts by weight) If the amount added is less than 0.001 parts by weight, the effect of the content may not be sufficiently obtained. This is preferable because the appearance of the shape tends to deteriorate.
- examples of powerful metal salts include organic acids such as acetic acid, propionic acid, butyric acid, lauric acid, stearic acid, oleic acid, and behenic acid, such as sodium, potassium, calcium, and magnesium, and sulfuric acid.
- metal salts of inorganic acids such as sulfurous acid, carbonic acid, and phosphoric acid are preferable, and acetate, phosphate, and hydrogen phosphate are preferable.
- the amount of the metal salt added is 0.0005-0. 1 parts by weight (more preferably 0.001-0.05 parts by weight, especially 0.002 part by weight) with respect to 100 parts by weight of EVOH. 0.03 parts by weight Weight of S is preferable, and the amount of added calorie is powerful.
- the amount is less than 5 parts by weight, the contained effect may not be obtained sufficiently, and conversely if it exceeds 0.1 parts by weight.
- the appearance of the resulting multilayer film tends to be poor, and is not preferable.
- the total amount is the same as that of the above additive. It is preferable to be in the range of soot amount.
- the method of adding an acid or a metal salt thereof to EVOH is not particularly limited.
- a porous precipitate of EVOH having a water content of 20 to 80% by weight is added to an acid or a metal salt thereof.
- C) EVOH and acids and their metal salts are mixed together in a batch using an extruder or the like.
- Melt-kneading method e During the production of EVOH, the alkali (sodium hydroxide, potassium hydroxide, etc.) used in the saponification process is neutralized with acids such as acetic acid, and the remaining acids and by-products such as acetic acid remain.
- the amount of alkali metal salt such as sodium acetate or potassium acetate How or adjusted by, and the like.
- the method of a), b) or d) which is excellent in dispersibility of acids and metal salts thereof is preferred.
- the EVOH composition obtained by the above methods a), b) or d) is dried after a salt or metal salt is added thereto.
- dryers for fluidized drying include cylinders, grooved agitation dryers, circular tube dryers, rotary dryers, fluidized bed dryers, vibrating fluidized bed dryers, and cone rotations.
- a dryer for performing static drying a batch type box dryer is used as a stationary material type, and a band dryer, a tunnel dryer, a rigid dryer is used as a material transfer type. Examples include mold dryers, but are not limited to these. It is also possible to combine fluidized drying and stationary drying.
- Air or an inert gas (nitrogen gas, helium gas, argon gas, etc.) is used as the heating gas used in the drying treatment, and the temperature of the heating gas is 40 to 150 ° C. It is preferable in terms of preventing thermal degradation of EVOH.
- the time required for the drying treatment is a force that depends on the water content of EVO H and its treatment amount, usually 15 minutes to 72 hours. It is preferred in terms of productivity and prevention of thermal degradation of EVO H.
- the ability of the EVOH composition to be dried under the above conditions is 0.001 to 5% by weight (more preferably 0.01 to 2% by weight, especially 0). If the water content is less than 0.001% by weight, the long run formability tends to decrease. Conversely, if the water content exceeds 5% by weight, It is preferable that foaming may occur during molding.
- EVOH or a composition thereof (hereinafter collectively referred to as an EVOH composition) used in the present invention can be obtained by force.
- some monomer residue (3,4 diol 1-butene, 3, 4 disiloxy 1-butene, 3 acyloxy 4-nonole 1-butene, 4-siloxy 3 all-one butene, 4, 5 diol 1 pentene, 4, 5 Diacyloxy 1 pentene, 4, 5 diol 3—Methyl-1 pentene, 4, 5 diol 3 -Methyl-1 pentene, 5, 6 diol 1 monohexene, 5, 6 diaxyloxy 1 hexene, 4, 5 disiloxy 2-methyl-1-butene, etc.) and monomer saponification products (3,4-diol -1-butene, 4, 5 diol 1 pentene, 4,5 diol 3-methyl-1 pentene, 4,5 diol 3-methyl-1 pentene, 5, 6 di diol
- EVOH used in the present invention is a blend of EVOH containing the structural unit (1) and other EVOH different from this, from the viewpoint of improving gas-noreness and pressure resistance.
- Other EVOHs that may be preferred include those with different structural units, those with different ethylene contents, those with different key degrees, and those with different molecular weights.
- Examples of EVOH that is different from EVOH having the structural unit (1) include EVOH, which only has an ethylene structural unit and a butyl alcohol structural unit, and a functional group such as a 2-hydroxyethoxy group in the side chain of EVOH. EVOH can be mentioned.
- the structural units may be the same or different, but the ethylene content difference is 1 mol% or more (more than 2 mol%, especially 2 ⁇ 20 mol%). If the excessive ethylene content difference is too large, transparency may be deteriorated, which is not preferable.
- melt flow rate (MFR) 210 ° C, load 2160g
- MFR melt flow rate
- LOOgZlO content further 0.5 ⁇ 50gZlO
- the EVOH and the composition thereof used in the present invention can be used for melt molding or the like as they are, but in the present invention, the powerful EVOH and the composition impede the purpose of the present invention.
- saturated fatty amide eg stearic acid amide
- unsaturated fatty acid amide eg oleic acid amide
- bis fatty acid amide eg ethylene bisstearic acid amide
- fatty acid metal salt eg calcium stearate, stearic acid
- Magnesium oxide, etc. low molecular weight polyolefin (for example, low molecular weight about 500-10,000)
- Lubricants such as molecular weight polyethylene or low molecular weight polypropylene
- inorganic salts for example, nodular talcite
- oxygen absorbers for example, reduced iron powders as inorganic oxygen absorbers, and water-absorbing substances
- the multilayer film of the present invention is laminated with other thermoplastic resin.
- a lamination method when laminating with another thermoplastic resin for example, a method of melt extrusion laminating another thermoplastic resin on the film, sheet or the like of the EVOH composition of the present invention through an adhesive resin.
- a method of melt extrusion laminating an EVOH composition to another thermoplastic resin film or sheet via an adhesive resin a method of co-extrusion of an EVOH composition and a thermoplastic resin via an adhesive resin
- the adhesiveness of the multilayer film is good and the productivity is high V, the co-extrusion method is preferred.
- co-extrusion method examples include a multi-one hold die method, a feed blow method, and the like.
- a known method such as a hook method, a multi-slot die method, or a die external bonding method can be employed.
- melt molding temperature at the time of melt extrusion is preferably 150 to 300 ° C.
- Polyolefin-based resin is useful as a strong thermoplastic resin.
- rosin is preferred from the viewpoint of practicality such as physical properties (particularly strength) of the multilayer film, polyethylene, polypropylene, and
- Arbitrary base materials paper, metal foil, uniaxial or biaxially stretched plastic film or sheet and its inorganic deposits, woven fabric, non-woven fabric, metallic cotton, wood, etc.
- thermoplastic resin woven fabric, non-woven fabric, metallic cotton, wood, etc.
- the layer structure of the multilayer film is such that when the EVOH-containing layer is a (al, a2,...) And the thermoplastic resin-containing layer is b (bl, b2,. BZaZb, a / b / a, al / a2 / b, a / bl / b2, b2 / bl / a / bl / b2, b 2 / b 1 / a / b 1 / a / b 1 / b 2 ⁇ Arbitrary combinations are possible, and when the regrind layer that also has a mixture power of at least the EVOH composition and thermoplastic resin is R, b / R / a, b / R / a / b, b / R / a / R / b, b / a / R / / b, bZRZaZRZaZRZb,
- a and b are bimetal type, core (a) — Arbitrary combinations such as sheath (b) type, core (b) -sheath (a) type, or eccentric core-sheath type are possible.
- an adhesive resin layer is disposed between the EVOH-containing layer and the thermoplastic resin-containing layer, and various types of adhesive resin can be used.
- the carboxyl group obtained by chemically bonding an unsaturated carboxylic acid or its anhydride to an olefin polymer (the above-mentioned polyolefin resin in the broad sense) by an addition reaction or a graft reaction is used.
- modified olefin-containing polymers examples include maleic anhydride graft-modified polyethylene, maleic anhydride graft-modified polypropylene, maleic anhydride graft-modified ethylene propylene (block and random) copolymer, anhydrous Maleic acid graft-modified ethylene ethyl acrylate copolymer, maleic anhydride graft-modified ethylene vinyl acetate copolymer, etc.
- One kind or a mixture of two or more kinds selected may be preferably mentioned.
- the amount of the unsaturated carboxylic acid or anhydride thereof contained in the thermoplastic resin is preferably 0.001 to 3% by weight, more preferably 0.01 to 1% by weight, and particularly preferably 0. 03 to 0.5% by weight. If the amount of modification in the modified product is small, the adhesiveness may be insufficient. On the other hand, if the amount is too large, a crosslinking reaction may occur and the moldability may be deteriorated.
- These adhesive resins can be blended with the EVOH composition of the present invention, other rubbers such as EVOH, polyisobutylene, and ethylene propylene rubber, an elastomer component, and b layer resin. is there.
- each layer of the multilayer film cannot be generally stated depending on the layer configuration, the type of b, the use and packaging form, the required physical properties, etc., but usually the a layer is 2 to 500 m (or 3 ⁇ 200 / ⁇ ⁇ ), b-layer is 10-5000 m (or 30-: L000 ⁇ m), the adhesive layer is about 1-400 m (or 2-150 ⁇ m) Selected.
- the oxygen permeability after bending test of the multilayer film obtained by force is 10 ccZm 2 .day • atm or less, and further 5 ccZm 2 ⁇ day ⁇ atm or less! /.
- the thermoplastic resin-containing layer may contain an antioxidant, an antistatic agent, a lubricant, a core material, an antiblocking agent, an ultraviolet absorber, a wax and the like as conventionally known.
- the multilayer film obtained by force is stretched according to its use and purpose, and used as a multilayer stretched film.
- This (heating) stretching treatment is an operation for uniformly forming a film or sheet-like laminate that has been heated uniformly into a tube or film by chucking, plug, vacuum force, pneumatic force, blow, or the like.
- a multilayer stretched film having excellent properties can be obtained.
- a roll stretching method a tenter stretching method, a tubular stretching method, a stretching blow method, a vacuum / pressure forming method, or the like can be employed.
- biaxial stretching both a simultaneous biaxial stretching method and a sequential biaxial stretching method can be employed.
- heat setting is performed.
- the heat setting can be performed by a known means, and the stretched film is kept in a tension state at 80 to 180 ° C, preferably 100 to
- Heat treatment is performed at 165 ° C for 2 to 600 seconds.
- each layer of the stretched multilayer film cannot be generally stated depending on the layer configuration, the type of b, the application and packaging form, the required physical properties, etc., but usually the a layer is 1 to 300 m (or 2 ⁇ 150 ⁇ m), b layer is 5 to 3000 m (or 15 to 500 ⁇ m), adhesive layer is about 0.5 to 200 m (or 1 to: LOO ⁇ m) Force selected.
- the oxygen permeability of the obtained multilayer stretched film at 23 ° C. and 80% RH is preferably 7 ccZ m 'dayatm or less, more preferably 6 ccz m' dayatm or less, particularly 5 cc / m 'dayatm or less.
- the multilayer film obtained by force has good gas noria properties, is excellent in adhesiveness, appearance, and bending resistance (gas barrier property after bending test), and is obtained by stretching the multilayer film.
- the resulting multilayer stretched film has good gas barrier properties and pinhole resistance.
- An lm 3 polymerization vessel with a cooling coil is charged with 500 kg of butyl acetate, 35 kg of methanol, 500 ppm of acetyl baroxide (vs. butyl acetate), 20 ppm of citrate, and 14 kg of 3,4 diacetoxy-1-butene.
- the mixture was injected until the ethylene pressure reached 5 kg / cm 2 , stirred, and then heated to 67 ° C to increase the temperature to 3, 4 diacetoxy-1-butene.
- the polymer was polymerized while adding 4.5 kg in a total amount of 15 gZ, and polymerized for 6 hours until the polymerization rate reached 50%. Thereafter, the polymerization reaction was stopped to obtain an ethylene-butyl acetate copolymer having an ethylene content of 38 mol%.
- a methanol solution of the ethylene acetate butyl copolymer was supplied at a rate of lOkgZ from the top of the plate tower (Ken ⁇ tower), and at the same time, with respect to the remaining acetic acid groups in the copolymer, 0. 01
- a methanol solution containing 2 equivalents of sodium hydroxide was fed from the top of the tower.
- methanol was supplied at 15 kgZ at the bottom of the tower.
- the tower temperature was 100-110 ° C and the tower pressure was 3kgZcm 2G.
- a methanol solution of EVOH (EVOH 30%, methanol 70%) having a structural unit having a 1,2 glycol bond was taken out.
- the saponification degree of the butyl acetate component of EVOH was 99.5 mol%.
- the obtained methanol solution of EVOH was supplied from the top of the methanol Z aqueous solution adjusting tower at lOkgZ, 120 ° C methanol vapor at 4kgZ, and steam at 2.5kg / hr. Charge from the bottom of the tower and distill methanol from the top of the tower at 8 kgZ. At the same time, 6 equivalents of methyl acetate with respect to the amount of sodium hydroxide used in Keni The middle force was also charged, and the bottom force was obtained as a water Z alcohol solution (wax concentration 35%) of EVOH.
- the obtained EVOH water Z alcohol solution was extruded in a strand form from a nozzle having a pore diameter of 4 mm into a coagulation liquid tank maintained at 5 ° C consisting of 5% methanol and 95% water.
- the strand was cut with a cutter to obtain E VOH porous pellets having a diameter of 3.8 mm and a length of 4 mm and a moisture content of 45%.
- the pellets After washing 100 parts of the porous pellets with 100 parts of water, the pellets were put into a mixed solution containing 0.032% boric acid and 0.007% calcium dihydrogen phosphate, and 5 ° C. at 30 ° C. Stir for hours. Furthermore, the porous pellets were heated in a batch-type ventilated box dryer at a temperature of 70 ° C and moisture content. After passing nitrogen gas with a content of 0.6% and drying for 12 hours to adjust the water content to 30%, using a batch tower fluid bed dryer, the temperature is 120 ° C and the water content is 0.5%. Drying with nitrogen gas for 12 hours yielded pellets of the desired EVOH composition.
- Such pellets contain 0.015 parts by weight (in terms of boron) and 0.005 parts by weight (in terms of phosphate group) of boric acid and calcium dihydrogen phosphate with respect to 100 parts by weight of EVOH, respectively, and MFR (210.C, 2160g) was 4. OgZlO.
- the amount of 1, 2 glycol bond introduced was calculated by measuring the ethylene vinyl acetate copolymer before saponification with 1 H-NMR (internal standard substance: tetramethylsilane, solvent: d6-DMSO). As a result, it was 2.5 mol%.
- “AV ANCE DPX400” manufactured by Nippon Bruker Co., Ltd. was used for NMR measurement.
- the integrated value of 1 proton is dZ4
- FIG. 2 shows the result of 1 H-NMR measurement performed on EVOH after Ken-ai. 1. Since the peak corresponding to 87 ppm to 2.06 ppm of methyl proton is greatly reduced, the copolymerized 3, 4 diacetoxy 1-butene is also kenned to form a 1, 2 glycol structure. It is clear that
- EVOH composition (A2) was obtained by the following method.
- EVOH composition (A3) was obtained by the following method.
- the amount of methanol used in Polymerization Example 1 is 20 kg, treated with a solution containing no boric acid, the ethylene content is 38 mol%, and the amount of structural units having 1,2 glycol bonds is 2.5 mol%.
- an ethylene content of 38 mole 0/0, saponification degree 99.5 mole 0/0, MFI 3. 5 g / min (210 ° C, 2160 g), the content of boric acid (boron conversion) 0 015 parts by weight, calcium dihydrogen phosphate
- the EVOH composition (A4) was prepared without containing 0.005 parts by weight (in terms of phosphate radical) of the structural unit (1).
- the EVOH composition (A1) obtained above is fed to a multilayer extruder equipped with 3 types of feed blocks, 3 layers, and 5 layers of multi-layer T-dies.
- Low density polyethylene Novatec LD LF441MD, layer Z adhesive resin
- Mitsubishi LD LF441MD layer Z adhesive resin
- the film was formed under conditions of a film forming speed of 20 mZ (low speed) and 50 mZ (high speed).
- the resulting multilayer film was evaluated in the following manner for adhesiveness, appearance, transparency, and pinhole resistance during high-speed film formation.
- X (g / 15mm) is the adhesive force between the EVOH layer and the adhesive resin layer when molded at a film forming speed of 20mZ, and the EVOH layer and adhesive resin layer when molded at a film forming speed of 50mZ.
- the adhesive strength was determined as Y (gZl5mm) based on the following criteria.
- the multilayer film obtained at a film forming speed of 50 mZ was evaluated by visual evaluation according to the following criteria.
- the multilayer film obtained at a film forming speed of 50 mZ was measured for haze with a haze meter and judged according to the following criteria.
- Haze value is less than 3 ⁇ : Haze value is 3 ⁇ 10
- the multilayer film obtained at a film-forming speed of 50 mZ was 440 ° twisted (3.5 inches) + straight ( 2.
- the oxygen permeability of the multilayer film was measured at 23 ° C and 80% RH using an oxygen permeability measuring device ("OXTRAN2Z21" manufactured by MOCON). (ccZm 2 'day atm) was measured.
- Example 1 a multilayer film was prepared in the same manner except that the EVOH composition (A2) was used instead of the EVOH composition (A1), and evaluation was performed in the same manner.
- Example 1 a multilayer film was prepared in the same manner except that the EVOH composition (A3) was used instead of the EVOH composition (A1), and evaluation was performed in the same manner.
- Example 1 a multilayer film was prepared and evaluated in the same manner except that the EVOH composition (A4) was used instead of the EVOH composition (A1).
- the unit of oxygen permeability is cc / m ⁇ day atm
- the obtained laminate was visually observed and the appearance was evaluated as follows.
- the oxygen permeability of the stretched multilayer film was measured using “OXTRAN2Z21” manufactured by MOCON under the conditions of 23 ° C. and 80% RH.
- the multilayer stretched film is used with a gelbo flex tester (manufactured by Rigaku Corporation) 23.
- a gelbo flex tester manufactured by Rigaku Corporation 23.
- OX CON2Z21 oxygen permeability measuring device manufactured by MO CON
- OX CON2Z21 oxygen permeability measuring device
- Example 4 a multilayer stretched film was prepared in the same manner except that the EVOH composition (A2) was used instead of the EVOH composition (A1), and evaluation was performed in the same manner.
- Example 4 a multilayer stretched film was prepared in the same manner except that the EVOH composition (A3) was used instead of the EVOH composition (A1), and evaluation was performed in the same manner. [0086] Comparative Example 2
- Example 1 a multilayer stretched film was prepared and evaluated in the same manner except that the EVOH composition (B1) was used instead of the EVOH composition (A1).
- Example 1 a multilayer stretched film was prepared in the same manner except that the EVOH composition (B2) was used instead of the EVOH composition (A1), and evaluation was performed in the same manner.
- Example 1 a multilayer stretched film was prepared in the same manner except that the EVOH composition (B3) was used instead of the EVOH composition (A2), and evaluation was performed in the same manner.
- Table 2 summarizes the evaluation results of Examples and Comparative Examples.
- the unit of gas barrier property is ccZm 2 'day atm
- the multilayer film and the multilayer stretched film of the present invention have a layer of EVOH containing the structural unit (1) having a 1,2-glycol bond in the side chain, and can exhibit adhesion, appearance, It has excellent transparency and pinhole resistance, and is useful as a packaging material for foods, medical products, industrial chemicals, chemicals, agricultural chemicals, electronic parts, and machine parts.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Laminated Bodies (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
Claims
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/JP2006/308673 WO2007129371A1 (ja) | 2006-04-25 | 2006-04-25 | 多層フィルム |
| EP06756327A EP2014462A4 (en) | 2006-04-25 | 2006-04-25 | MULTILAYER FILM |
| US12/226,692 US20090311524A1 (en) | 2006-04-25 | 2006-04-25 | Multi-Layer Film |
| CNA2006800543660A CN101448639A (zh) | 2006-04-25 | 2006-04-25 | 多层膜 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/JP2006/308673 WO2007129371A1 (ja) | 2006-04-25 | 2006-04-25 | 多層フィルム |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2007129371A1 true WO2007129371A1 (ja) | 2007-11-15 |
Family
ID=38667492
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2006/308673 Ceased WO2007129371A1 (ja) | 2006-04-25 | 2006-04-25 | 多層フィルム |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US20090311524A1 (ja) |
| EP (1) | EP2014462A4 (ja) |
| CN (1) | CN101448639A (ja) |
| WO (1) | WO2007129371A1 (ja) |
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| JP2014531341A (ja) * | 2011-09-20 | 2014-11-27 | テトラ・ラヴァル・ホールディングス・アンド・ファイナンス・ソシエテ・アノニムTetra Laval Holdings & Finance S.A. | 多層バリアフィルム、そのフィルムを含むパッケージングラミネート、そのパッケージングラミネートから形成されるパッケージング容器、及びそのフィルムの製造方法 |
| US9873238B2 (en) | 2009-12-01 | 2018-01-23 | Kuraray Co., Ltd. | Inner liner for pneumatic tire and method for producing the same |
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| CN106795232B (zh) * | 2014-07-11 | 2019-04-23 | 株式会社可乐丽 | 乙烯-乙烯醇共聚物、树脂组合物、及使用了它们的成型体 |
| EP3272525B1 (en) * | 2015-03-18 | 2023-02-08 | Mitsubishi Chemical Corporation | Multilayer structure, and packaging material formed from the multilayer structure |
| CN106476384A (zh) * | 2016-12-09 | 2017-03-08 | 闽南师范大学 | 一种新型环保型高阻隔cpp薄膜及其制备方法 |
| JP7151482B2 (ja) * | 2017-06-27 | 2022-10-12 | 三菱ケミカル株式会社 | エチレン-ビニルアルコール系共重合体組成物、ペレット、多層構造体、および多層パイプ |
| EP3873739A1 (en) | 2020-01-06 | 2021-09-08 | Flint Hills Resources, LP | Polymeric substrate including a barrier layer |
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| EP2107570A1 (en) * | 2008-03-31 | 2009-10-07 | Hitachi Global Storage Technologies Netherlands B.V. | Scheme to protect media and head against corrosion/oxidation in a hard disk drive |
| JPWO2011068105A1 (ja) * | 2009-12-01 | 2013-04-18 | 株式会社クラレ | 多層構造体及びその製造方法 |
| US9186873B2 (en) | 2009-12-01 | 2015-11-17 | Kuraray Co., Ltd. | Multilayered structure and method for producing the same |
| US9873238B2 (en) | 2009-12-01 | 2018-01-23 | Kuraray Co., Ltd. | Inner liner for pneumatic tire and method for producing the same |
| JP2014531341A (ja) * | 2011-09-20 | 2014-11-27 | テトラ・ラヴァル・ホールディングス・アンド・ファイナンス・ソシエテ・アノニムTetra Laval Holdings & Finance S.A. | 多層バリアフィルム、そのフィルムを含むパッケージングラミネート、そのパッケージングラミネートから形成されるパッケージング容器、及びそのフィルムの製造方法 |
| WO2024085228A1 (ja) * | 2022-10-21 | 2024-04-25 | 株式会社クラレ | 多層フィルム、包装材及び反応装置 |
| WO2025029960A1 (en) * | 2023-08-01 | 2025-02-06 | Signode Industrial Group Llc | Multilayer stretch films |
Also Published As
| Publication number | Publication date |
|---|---|
| US20090311524A1 (en) | 2009-12-17 |
| CN101448639A (zh) | 2009-06-03 |
| EP2014462A4 (en) | 2010-02-10 |
| EP2014462A1 (en) | 2009-01-14 |
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