WO2017110568A1 - Resin composition and molded article - Google Patents

Resin composition and molded article Download PDF

Info

Publication number
WO2017110568A1
WO2017110568A1 PCT/JP2016/086951 JP2016086951W WO2017110568A1 WO 2017110568 A1 WO2017110568 A1 WO 2017110568A1 JP 2016086951 W JP2016086951 W JP 2016086951W WO 2017110568 A1 WO2017110568 A1 WO 2017110568A1
Authority
WO
WIPO (PCT)
Prior art keywords
resin composition
metal salt
ppm
acid
evoh
Prior art date
Application number
PCT/JP2016/086951
Other languages
French (fr)
Japanese (ja)
Inventor
義和 山崎
英里子 米谷
Original Assignee
株式会社クラレ
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 株式会社クラレ filed Critical 株式会社クラレ
Priority to CN201680075588.4A priority Critical patent/CN108473744B/en
Priority to JP2017557889A priority patent/JP6704415B2/en
Publication of WO2017110568A1 publication Critical patent/WO2017110568A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/32Phosphorus-containing compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K13/00Use of mixtures of ingredients not covered by one single of the preceding main groups, each of these compounds being essential
    • C08K13/02Organic and inorganic ingredients
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/38Boron-containing compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/04Oxygen-containing compounds
    • C08K5/09Carboxylic acids; Metal salts thereof; Anhydrides thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/49Phosphorus-containing compounds
    • C08K5/51Phosphorus bound to oxygen
    • C08K5/53Phosphorus bound to oxygen bound to oxygen and to carbon only
    • C08K5/5317Phosphonic compounds, e.g. R—P(:O)(OR')2
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/55Boron-containing compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L29/00Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical; Compositions of hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Compositions of derivatives of such polymers
    • C08L29/02Homopolymers or copolymers of unsaturated alcohols
    • C08L29/04Polyvinyl alcohol; Partially hydrolysed homopolymers or copolymers of esters of unsaturated alcohols with saturated carboxylic acids

Definitions

  • the present invention relates to a resin composition and a molded body.
  • EVOH ethylene-vinyl alcohol copolymer
  • These packaging materials are usually molded by a melt molding method, and EVOH is required to have excellent appearance characteristics (low coloration such as yellowing) and excellent long-run property during melt molding.
  • the packaging material is often configured as a multilayer structure, but may be an EVOH resin composition containing metal ions in EVOH in order to improve interlayer adhesion of the multilayer structure.
  • metal ions when metal ions are contained in EVOH, coloring tends to occur, resulting in a disadvantage that the appearance characteristics of the molded body are deteriorated.
  • EVOH has a large number of highly reactive hydroxyl groups in its molecular structure. For this reason, when EVOH is operated continuously for a long time, defects such as gels and blisters increase over time, and streaky appearance defects increase over time, resulting in commercial value as a molded product. Has a problem related to long-run properties such as a decrease in In addition, about long run problems such as the increase in gels and blisters and the appearance of streaky appearance, which problem occurs depends on the equipment and operating conditions used for molding, both problems May occur. In any case, such an EVOH resin composition excellent in long run properties with little change with time even in continuous operation for a long time is desired.
  • JP-A-64-66262 discloses an EVOH resin composition containing an acid such as a carboxylic acid and a metal ion.
  • Japanese Patent No. 5619874 describes an EVOH resin composition containing a polyvalent carboxylic acid and a metal ion. These EVOH resin compositions are said to be excellent in appearance characteristics and long run properties.
  • JP-A 64-66262 Japanese Patent No. 5619874
  • the present invention has been made on the basis of the circumstances as described above, and has excellent appearance characteristics and long run properties in melt molding, and can suppress the occurrence of yellowing even after repeated reuse. It aims at providing the composition and the molded object obtained using such a composition.
  • the invention made in order to solve the above problems is a resin composition containing EVOH as a main component, containing a phosphorus compound and a metal salt, wherein the phosphorus compound is condensed phosphoric acid, two or more phosphonic acid groups Or a combination thereof, wherein the phosphorus compound content is 0.1 ppm or more and less than 50 ppm, and the metal salt content is 5 ppm or more and 500 ppm or less in terms of metal element.
  • the resin composition is considered to cause yellowing or the like by setting the content of a specific phosphorous compound that is condensed phosphoric acid, a compound having two or more phosphonic acid groups, or a combination thereof in the above range. It is considered that a phosphate group or a phosphonic acid group is stably coordinated with a metal ion and can incorporate the metal ion. That is, the presence of metal ions in a coordinated state in this manner can suppress the catalytic function for reactions such as yellowing of EVOH possessed by metal ions, and as a result, repeated reuse. Even in such a case, the occurrence of coloring such as yellowing can be suppressed.
  • the resin composition contains a metal salt in the above range, defects such as gels and blisters do not increase over time even during long-time molding, or streaky appearance defects even during long-time molding. Can exhibit an excellent long-run property such that does not increase with time.
  • the metal salt is preferably an alkali metal salt, an alkaline earth metal salt, or a combination thereof.
  • the metal salt is preferably an alkali metal salt.
  • the alkali metal salt can suitably exhibit a long run property such that defects such as gels and blisters do not increase with time even during long-time molding.
  • the metal salt is an alkaline earth metal salt, and the content of the alkaline earth metal salt is 5 ppm or more and 100 ppm or less in terms of metal element.
  • the alkaline earth metal salt can exhibit a long run property such that a streak-like appearance defect does not increase with time even in a long-time molding.
  • the resin composition further contains a monocarboxylic acid, and the content of the monocarboxylic acid is preferably 5 ppm or more and 500 ppm or less.
  • the said resin composition contains a boron compound further, and it is preferable that content of the said boron compound is 5 ppm or more and 2,000 ppm or less in conversion of a boron element.
  • the molded product of the present invention is a molded product having a part formed from the resin composition. Since the molded body is provided with a portion obtained from the resin composition having excellent appearance characteristics and long run properties as described above, the occurrence of coloring such as yellowing, gel, butts, fish eyes, and streaks is suppressed. It has a good appearance.
  • a resin composition having excellent appearance characteristics and long run property in melt molding, and particularly capable of suppressing the occurrence of yellowing even after repeated reuse, and such a composition are used. It is possible to provide a molded product obtained in this way.
  • the resin composition of the present invention contains EVOH as a main component and a phosphorus compound and a metal salt.
  • a main component means a component with most content on a mass basis.
  • EVOH EVOH is a copolymer having ethylene units and vinyl alcohol units. However, this EVOH may contain one or more other structural units.
  • EVOH can be produced by a known method.
  • ethylene unit content of EVOH 15 mol% is preferred, 20 mol% is more preferred, and 25 mol% is still more preferred.
  • the upper limit of the ethylene unit content of EVOH is preferably 60 mol%, more preferably 55 mol%, and even more preferably 50 mol%.
  • the ethylene unit content of EVOH is smaller than the above lower limit, the long-run property of the resin composition, the water resistance, hot water resistance and gas barrier property under high humidity of the resulting molded product may be deteriorated.
  • the ethylene unit content of EVOH exceeds the above upper limit, the gas barrier property and the like of the resulting molded article may be lowered.
  • the lower limit of the saponification degree of EVOH is preferably 80 mol%, more preferably 95 mol%, and even more preferably 99 mol%. If the saponification degree of EVOH is smaller than the above lower limit, the gas barrier properties and appearance characteristics of the obtained molded product may be deteriorated.
  • EVOH is usually obtained by saponifying an ethylene-vinyl ester copolymer obtained by copolymerizing ethylene and a vinyl ester.
  • the polymerization of ethylene and vinyl ester may be carried out by any known method such as solution polymerization, suspension polymerization, emulsion polymerization, bulk polymerization, etc., and may be either continuous type or batch type.
  • the polymerization conditions in the case of solution polymerization are as follows.
  • Alcohols are preferable, but other organic solvents (such as dimethyl sulfoxide) that can dissolve ethylene, vinyl ester, and ethylene-vinyl ester copolymer can be used.
  • organic solvents such as dimethyl sulfoxide
  • methyl alcohol, ethyl alcohol, propyl alcohol, n-butyl alcohol, t-butyl alcohol and the like can be used, and methyl alcohol is particularly preferable.
  • Polymerization initiator 2,2'-azobisisobutyronitrile, 2,2'-azobis- (2,4-dimethylvaleronitrile), 2,2'-azobis- (4-methoxy-2,4-dimethyl) Valeronitrile), azonitrile initiators such as 2,2′-azobis- (2-cyclopropylpropionitrile), isobutyryl peroxide, cumylperoxyneodecanoate, diisopropylperoxycarbonate, di-n-propyl Organic peroxide initiators such as peroxydicarbonate, dicyclohexylperoxydicarbonate, t-butylperoxyneodecanoate, lauroyl peroxide, benzoyl peroxide, t-butyl hydroperoxide, diacetyl peroxide, etc. Can be used.
  • Temperature 20 ° C. or higher and 90 ° C. or lower, preferably 40 ° C. or higher and 70 ° C. or lower.
  • Time 2 hours to 15 hours, preferably 3 hours to 11 hours.
  • Polymerization rate 10% to 90%, preferably 30% to 80% with respect to the charged vinyl ester.
  • Resin content in the solution after polymerization 5% to 85%, preferably 20% to 70%.
  • Typical vinyl esters used for polymerization include vinyl acetate, but other aliphatic vinyl esters such as vinyl formate, vinyl propionate, vinyl butyrate, vinyl isobutyrate, vinyl pivalate, vinyl versatate, capron. Examples include vinyl acid.
  • ethylenically unsaturated monomers that can be copolymerized can be copolymerized in a small amount as long as the effects of the present invention are not inhibited.
  • ethylenically unsaturated monomers include ⁇ -olefins such as propylene, n-butene, isobutylene and 1-hexene; Unsaturated monomers having 1,2-diester groups such as 3,4-diacetoxy-1-butene; 2-methylene-1,3-propanediol diacetate (1,3-diacetoxy-2-methylenepropane), 2-methylene-1,3-propanediol dipropionate, 2-methylene-1,3-propanediol dibuty Unsaturated monomers having a 1,3-diester group such as a rate; Acrylic acid and its salts; An unsaturated monomer having an acrylate group; Methacrylic acid and its salts; An unsaturated monomer
  • Vinyl ethers Vinyl cyanides such as acrylonitrile and methacrylonitrile; vinyl halides such as vinyl chloride and vinyl fluoride; Vinylidene halides such as vinylidene chloride and vinylidene fluoride; Allyl compounds such as allyl acetate, 2,3-diacetoxy-1-allyloxypropane, allyl chloride; Unsaturated dicarboxylic acids such as maleic acid, itaconic acid, fumaric acid, and salts or esters thereof; Vinylsilane compounds such as vinyltrimethoxysilane; And isopropenyl acetate.
  • a polymerization inhibitor is added as necessary, and after removing unreacted ethylene gas, unreacted vinyl ester is removed.
  • the copolymer solution is continuously supplied at a constant rate from the upper part of a column packed with Raschig rings, An ethylene-vinyl ester copolymer solution in which an organic solvent vapor such as methanol is blown from the bottom of the column, a mixed vapor of an organic solvent such as methanol and unreacted vinyl ester is distilled from the top of the column, and the unreacted vinyl ester is removed from the bottom of the column.
  • the method of taking out is adopted.
  • the saponification of the ethylene-vinyl ester copolymer is performed by a known method such as acid saponification or alkali saponification.
  • a known method such as acid saponification or alkali saponification.
  • an alkali catalyst is added to the copolymer solution from which the unreacted ethylene and unreacted vinyl ester obtained above are removed, and the vinyl ester portion in the copolymer is saponified.
  • the saponification method can be either a continuous type or a batch type.
  • As the alkali catalyst sodium hydroxide, potassium hydroxide, alkali metal alcoholate or the like is used, and the following conditions are preferably used.
  • Copolymer solution concentration 10% or more and 50% or less.
  • Reaction temperature 30 ° C or higher and 60 ° C or lower.
  • Catalyst usage 0.02 equivalents to 0.6 equivalents (per vinyl ester component). Time: 1 hour 6 hours or less.
  • the thus obtained EVOH after the saponification reaction contains catalyst residues, by-product salts, and other impurities used in the saponification reaction, and is removed by neutralization and washing as necessary. It is preferable.
  • the lower limit of the EVOH melt flow rate (according to JIS K 7210, temperature 210 ° C., load 2160 g, hereinafter abbreviated as MFR) is preferably 0.1 g / 10 minutes, preferably 0.5 g / 10. Minute is more preferable, 1 g / 10 minutes is further more preferable, and 3 g / 10 minutes is particularly preferable.
  • the upper limit of MFR of EVOH is preferably 200 g / 10 minutes, more preferably 50 g / 10 minutes, further preferably 30 g / 10 minutes, still more preferably 15 g / 10 minutes, and particularly preferably 10 g / 10 minutes.
  • the lower limit of the EVOH content in the resin composition is, for example, preferably 80% by mass, and more preferably 90% by mass. Furthermore, 99 mass% may be sufficient as the minimum of content of EVOH, and 99.9 mass% may be sufficient as it.
  • content of EVOH is equal to or more than the above lower limit, the obtained molded body can exhibit various characteristics of EVOH more effectively.
  • content of each component in the said resin composition is a ratio with respect to the whole dried resin composition (hereinafter the same).
  • the resin composition contains a specific phosphorus compound.
  • the phosphorus compound is condensed phosphoric acid, a compound having two or more phosphonic acid groups (—P (O) (OH) 2 ), or a combination thereof. That is, as this phosphorus compound, only one type of condensed phosphoric acid, a compound having two or more phosphonic acid groups may be used, or a plurality of types may be used in combination.
  • the resin composition is not affected by other components constituting the resin composition, and yellowing occurs after melt molding and after repeated reuse. Can be suppressed. It is considered that a condensed phosphoric acid or a phosphorus compound having two or more phosphonic acid groups can stably coordinate to a metal ion that is responsible for yellowing or the like and take in the metal ion. It is presumed that the phosphorus compound is stably present in a coordinated state with the metal ion, thereby suppressing the action of the metal ion that catalytically promotes the decomposition and coloring of EVOH.
  • condensed phosphoric acid examples include pyrophosphoric acid (also called diphosphoric acid), tripolyphosphoric acid, tetrapolyphosphoric acid, and the like, and pyrophosphoric acid is preferred.
  • the compound having two or more phosphonic acid groups include etidronic acid (also referred to as 1-hydroxyethane-1,1-diphosphonic acid), alendronic acid, nitrotris (methylenephosphonic acid), ethylenediaminetetra (methylenephosphonic acid) Among them, etidronic acid and alendronic acid are preferable.
  • the condensed phosphoric acid may or may not have two or more phosphonic acid groups.
  • the compound having two or more phosphonic acid groups may contain condensed phosphoric acid having two or more phosphonic acid groups.
  • the compound having two or more phosphonic acid groups may be a compound other than condensed phosphoric acid having two or more phosphonic acid groups.
  • phosphorus compounds may exist in the state of oxygen acid, or may exist as phosphates or phosphonates that form salts with counter cations such as metal ions. Moreover, a hydrate may be sufficient. In the resin composition, it may be dissociated as ions or not.
  • the phosphate any of the first phosphate, the second phosphate and the third phosphate may be used.
  • As the phosphonate either the first phosphonate or the second phosphonate may be used. It may be in the form.
  • the counter cation species is not particularly limited. When a phosphorus compound that forms a salt with a metal ion of a counter cation is mixed, the metal ion also acts as a metal ion in a metal salt described later.
  • the molecular weight of this phosphorus compound is not particularly limited, but the upper limit is preferably 1,000, for example, and more preferably 600. On the other hand, the lower limit is 170, for example. By being a compound having a molecular weight within the above range, more stable coordination to a metal ion is possible, and the ability to suppress yellowing is increased.
  • the number of phosphoric acid groups (—O—P (O) (OH) 2 ) and phosphonic acid groups possessed by the phosphorus compound is 2 or more, and the upper limit is, for example, 6 and 4 is preferable, 3 is more preferable, and 2 is more preferable.
  • the number of the phosphoric acid group and the phosphonic acid group that the phosphorus compound has is within the above range, more stable coordination to the metal ion is possible, and the ability to suppress yellowing is increased.
  • the lower limit of the content of the phosphorus compound is 0.1 ppm, preferably 0.5 ppm, more preferably 3 ppm, still more preferably 10 ppm, and particularly preferably 20 ppm.
  • the content of this phosphorus compound is less than 50 ppm, preferably less than 45 ppm, and more preferably less than 35 ppm.
  • the resin composition contains a metal salt.
  • the metal salt include alkali metal salts, alkaline earth metal salts, and other transition metal salts, and may be a single metal species, or may be composed of a plurality of these metal species. good.
  • an alkali metal salt, alkaline-earth metal salt, or these combination is preferable.
  • this metal salt does not include a metal salt of the specific phosphorus compound (a compound having two or more condensed phosphoric acid and phosphonic acid groups).
  • the lower limit of the metal element equivalent amount of the metal salt is 5 ppm, preferably 30 ppm, more preferably 50 ppm, and 100 ppm with respect to the entire resin composition.
  • the upper limit of the metal element equivalent amount of the metal salt is 500 ppm, preferably 400 ppm, more preferably 300 ppm, and may be 200 ppm.
  • the resin composition in which the metal salt is an alkali metal salt is preferable in that an increase in generation of defects such as gels and bumps with time is suppressed even during long-time molding.
  • the alkali metal that forms the alkali metal salt include lithium, sodium, and potassium, and sodium and potassium are preferable.
  • the alkali metal salt include aliphatic carboxylates such as lithium, sodium, and potassium, aromatic carboxylates, carbonates, hydrochlorides, nitrates, sulfates, phosphates, metal complexes, and the like. Among these, sodium acetate, potassium acetate, sodium carbonate, potassium carbonate, sodium phosphate and potassium phosphate are more preferable because they are easily available.
  • the lower limit of the content of the alkali metal salt in terms of metal element is preferably 5 ppm, more preferably 50 ppm, and even more preferably 100 ppm with respect to the entire resin composition.
  • the upper limit of the content of alkali metal salt in terms of metal element is 500 ppm, preferably 400 ppm, and more preferably 300 ppm.
  • a resin composition in which the metal salt contains an alkaline earth metal salt is preferable in that an increase in the appearance of streaky appearance over time is suppressed even during long-time molding.
  • the alkaline earth metal salt include salts of beryllium, magnesium, calcium, strontium, barium and the like.
  • Magnesium salts and calcium salts are preferred from the viewpoint of industrial availability, aliphatic carboxylates, aromatic carboxylates, carbonates, hydrochlorides, nitrates, sulfates, phosphates, metal complexes, etc. Is mentioned.
  • the lower limit of the content of the alkaline earth metal salt in terms of metal element is preferably 5 ppm, more preferably 30 ppm, based on the entire resin composition.
  • the upper limit of the content of the alkaline earth metal salt in terms of metal element may be 150 ppm, but is preferably 100 ppm, and more preferably 80 ppm.
  • the lower limit of the phosphorus compound content ratio (phosphorus compound / metal salt) to the metal salt content (in terms of metal element) in the resin composition is preferably 0.001, more preferably 0.005, 0.01 is more preferable, 0.05 is particularly preferable, and 0.1 is further particularly preferable. Further, when the metal salt is an alkaline earth metal salt, the lower limit of this ratio is more preferably 0.3. On the other hand, the upper limit of this ratio is preferably, for example, 5 and more preferably 1. Furthermore, when the metal salt is an alkali metal salt, the upper limit of this ratio is more preferably 0.5, and even more preferably 0.3.
  • the resin composition may contain a monocarboxylic acid.
  • a monocarboxylic acid is a compound having one carboxy group in the molecule.
  • the content of monocarboxylic acid is preferably 500 ppm or less, more preferably 300 ppm or less, based on the entire resin composition from the viewpoint of reducing odor.
  • the monocarboxylic acid content is not more than the above upper limit, the odor generated when the resin composition is melt-molded is reduced in addition to the odor of the resin composition itself, so that the working environment is reduced. Improved.
  • the molded article using the resin composition is particularly suitable for contents such as cooked rice and drinking water in which odor generation impairs the commercial value. Can also be preferably used as a packaging material.
  • the content of the monocarboxylic acid is preferably 5 ppm or more, more preferably 50 ppm or more with respect to the entire resin composition from the viewpoint of quality stability.
  • the content of the monocarboxylic acid is not less than the above lower limit, the pH of the aqueous solution can be easily controlled during the production of the resin composition, and it becomes easy to obtain a product with stable quality.
  • Examples of the monocarboxylic acid include formic acid, acetic acid, propionic acid, butyric acid, caproic acid, capric acid, acrylic acid, methacrylic acid, benzoic acid, and 2-naphthoic acid.
  • acetic acid is preferable.
  • These monocarboxylic acids may have a hydroxy group or a halogen atom.
  • the resin composition may contain a boron compound.
  • the boron compound include boric acid, boric acid ester, borate, and borohydride.
  • boric acid include orthoboric acid (H 3 BO 3 ), metaboric acid, and tetraboric acid.
  • boric acid esters include triethyl borate and trimethyl borate.
  • the salt include alkali metal salts, alkaline earth metal salts, borax and the like of the various boric acids described above. Of these, orthoboric acid is preferred.
  • the lower limit of the boron compound content of the boron compound is preferably 5 ppm, more preferably 10 ppm, based on the entire resin composition.
  • the upper limit of the boron element content of the boron compound is preferably 2,000 ppm, more preferably 1,000 ppm, and even more preferably 500 ppm.
  • the resin composition may contain an appropriate amount of components other than the above-described EVOH, phosphorus compound, metal salt, monocarboxylic acid, and boron compound as long as the effects of the present invention are not impaired.
  • other components include a plasticizer, a stabilizer, a surfactant, a colorant, an ultraviolet absorber, a slip agent, an antistatic agent, a drying agent, a crosslinking agent, a filler, an oxygen absorber, and various fibers. Can be mentioned.
  • the content of these additives (components other than EVOH, phosphorus compound, metal salt, monocarboxylic acid and boron compound) in the resin composition is less than 10% by mass, less than 1% by mass, and further 0.1% by mass. %.
  • thermoplastic resin other than EVOH
  • examples of the thermoplastic resin include various polyolefins (polyethylene, polypropylene, poly (1-butene), poly (4-methyl-1-pentene), ethylene-propylene copolymer, ethylene and ⁇ -olefin having 4 or more carbon atoms.
  • the resin composition contains a thermoplastic resin other than EVOH
  • the blending amount is preferably less than 50% by mass, more preferably less than 30% by mass, further preferably less than 10% by mass, and even more preferably less than 1% by mass. Preferably, it may be less than 0.1% by mass.
  • the preferable range of MFR of the resin composition is the same as that of the above-mentioned MFR of EVOH, and the effect obtained by setting the range is the same as that of EVOH.
  • the resin composition can be formed into various molded bodies such as pellets, films, sheets, containers, pipes and fibers by melt molding.
  • the resin composition includes, for example, a copolymerization step (step 1) in which ethylene and vinyl ester are copolymerized to obtain an ethylene-vinyl ester copolymer, and EVOH is obtained by saponifying the ethylene-vinyl ester copolymer.
  • the production method includes a saponification step (step 2), and further includes a mixing step (step ⁇ ) of mixing the ethylene-vinyl ester copolymer or EVOH with the phosphorus compound and metal salt after the copolymerization step. Can be obtained.
  • the phosphorus compound and the metal salt may be mixed simultaneously or separately.
  • Step 1 Copolymerization step
  • a polymerization inhibitor is added as necessary, and then unreacted ethylene and unreacted vinyl ester are removed to remove ethylene-vinyl ester copolymer. Obtaining a coalesced solution.
  • the copolymerization method of ethylene and vinyl ester include known methods such as solution polymerization, suspension polymerization, emulsion polymerization, and bulk polymerization. Specific polymerization conditions and the like are as described above for the EVOH production method.
  • this mixing step for example, (1) a method of previously adding the phosphorus compound to a solution containing an ethylene-vinyl ester copolymer used for the saponification step, (2) A method of adding the phosphorus compound during the saponification reaction of the ethylene-vinyl ester copolymer in the saponification step, and (3) a method of mixing the phosphorus compound after obtaining EVOH in the saponification step. .
  • a granulation step may be provided after the copolymerization step and the saponification step. Since EVOH is obtained in the form of a solution containing the solvent used in the saponification reaction, washing is performed in order to remove a catalyst such as alkali and a by-product such as sodium acetate remaining in the solution. In order to facilitate this washing operation, it is preferable to granulate the EVOH-containing solution obtained in the saponification step into EVOH hydrous pellets.
  • granulation operations for example, (I) a method in which an EVOH-containing solution is extruded into a coagulation bath and is cooled and solidified or cut immediately after, or (II) the EVOH solution is brought into contact with water vapor in advance to contain EVOH-containing water.
  • the method of cutting as a resin composition is mentioned.
  • the moisture content of the EVOH hydrous pellets obtained by these methods is preferably 40% by mass or more and 200% by mass or less based on the dry mass of EVOH.
  • the EVOH hydrous pellets obtained in the granulation step are preferably dried to form EVOH dry pellets.
  • the moisture content in the dry pellets is preferably 1.0% by mass or less and 0.8% by mass or less with respect to the entire dry pellets for the purpose of preventing molding troubles such as generation of voids during molding. Is more preferably 0.5% by mass or less.
  • Examples of the method for drying the water-containing pellets include stationary drying and fluidized drying. These drying methods may be used alone or in combination.
  • the drying treatment may be performed by either a continuous method or a batch method.
  • a continuous type and a batch type can be freely selected about each drying method. It is also preferable to perform the drying at a low oxygen concentration or an oxygen-free state from the viewpoint that the deterioration of the resin composition due to oxygen during drying can be reduced.
  • the mixing step may be performed after granulation.
  • a method of mixing a phosphorus compound or the like after the granulation step for example, (1) a method of bringing a water-containing pellet of EVOH into contact with a solution containing the phosphorus compound or the like, and (2) a water-containing pellet of EVOH and the phosphorus compound And the like are melt kneaded in an extruder.
  • monocarboxylic acid, alkali metal salt, alkaline earth metal salt, boron compound and the like can be mixed with EVOH at the same time.
  • the shape of the water-containing pellet is arbitrary, and the operation may be either a batch method or a continuous method.
  • the immersion may be divided into a plurality of solutions in which each component to be contained in the resin composition is individually dissolved, or may be processed at once using a solution in which a plurality of components are dissolved.
  • the said molded object is a molded object which has a part formed from the said resin composition.
  • the said molded object may be formed only from the said resin composition, for example, a laminated body etc. which have a part formed from the said EVOH resin in part may be sufficient as it.
  • the molded body examples include pellets, films, sheets, containers, pipes, fibers, and the like.
  • the molded body is usually molded by melt molding of the resin composition. These molded bodies can be pulverized and molded again for the purpose of reuse. It is also possible to uniaxially or biaxially stretch films, sheets, fibers, and the like.
  • melt molding method for example, any known molding method such as extrusion molding, inflation extrusion, blow molding, melt spinning, and injection molding can be applied.
  • the melting temperature at the time of melt molding is preferably about 150 ° C. or more and 300 ° C. or less, and usually a melting temperature of about 200 ° C. or more and 250 ° C. or less is employed.
  • the molded body thus obtained has excellent appearance characteristics in which coloring such as yellowing after melt molding is suppressed and gel, butts, fish eyes, streaks and the like are suppressed.
  • the molded body may be a multilayer structure including at least one layer obtained from the resin composition. Since the multilayer structure has a layer obtained from a resin composition having excellent appearance characteristics and long run properties, coloring such as yellowing, generation of gels and blisters, fish eyes and stripes are suppressed. Has excellent appearance characteristics.
  • the layer structure of the multilayer structure for example, when the layer obtained from the resin composition is represented by E, the layer obtained from the adhesive resin is represented by Ad, and the layer obtained from the thermoplastic resin is represented by T, T / E / T, E / Ad / T, and T / Ad / E / Ad / T.
  • E the layer obtained from the resin composition
  • Ad the layer obtained from the adhesive resin
  • T the layer obtained from the thermoplastic resin
  • the adhesive resin examples include an adhesive resin containing a carboxylic acid-modified polyolefin.
  • a carboxylic acid-modified polyolefin a modified olefin containing a carboxyl group obtained by chemically bonding an ethylenically unsaturated carboxylic acid, its ester or its anhydride to an olefin polymer (for example, addition reaction, graft reaction, etc.)
  • a polymer can be preferably used.
  • Examples of the ethylenically unsaturated carboxylic acid, its ester or its anhydride include maleic acid, fumaric acid, itaconic acid, maleic anhydride, itaconic anhydride, maleic acid monomethyl ester, maleic acid monoethyl ester, maleic acid diethyl ester, fumaric acid Acid monomethyl ester and the like, and maleic anhydride is more preferable.
  • These adhesive resins may be used alone or in admixture of two or more.
  • thermoplastic resin examples include linear low density polyethylene, low density polyethylene, medium density polyethylene, high density polyethylene, ethylene-vinyl acetate copolymer, ethylene-propylene copolymer, polypropylene, propylene- ⁇ -olefin copolymer
  • Polyolefins such as polymers, polybutenes, polypentenes or copolymers thereof; polyesters such as polyethylene terephthalate; polyester elastomers; polyamides such as nylon 6 and nylon 66; polystyrenes; polyvinyl chloride; polyvinylidene chloride; Resin, polyurethane elastomer, polycarbonate, chlorinated polyethylene, and chlorinated polypropylene.
  • polypropylene, polyethylene, ethylene-propylene copolymer, ethylene-vinyl acetate copolymer, polyamide, polystyrene and polyester are preferably used.
  • Examples of the method for producing the multilayer structure include the following methods. (1) Method of melt-extruding a thermoplastic resin on a molded body obtained from the resin composition (2) Method of co-extruding the resin composition and another thermoplastic resin (3) The resin composition and heat Method of co-injecting a plastic resin (4) Method of laminating a molded body obtained from the resin composition and another substrate using an adhesive
  • the method (2) can be preferably used. This is because the resin composition of the present invention is excellent in long run properties even when melted under high temperature conditions, and subsequent coloring is also suppressed, so even if it is co-extruded with other thermoplastic resins having a high melting point, It is because coloring can be suppressed and a multilayer structure excellent in appearance characteristics can be obtained.
  • the co-extrusion method include a multi-manifold joining method T-die method, a feed block joining method T-die method, and an inflation method.
  • the following molded body is obtained.
  • a multilayer stretched sheet or film obtained by stretching and heat-treating a multilayer structure (sheet or film, etc.) in a uniaxial or biaxial direction.
  • Multi-layer rolled sheet or film obtained by rolling a multilayer structure (sheet or film, etc.).
  • Multi-layer tray or cup-shaped container obtained by thermoforming a multi-layer structure (sheet or film, etc.) such as vacuum forming, pressure forming, vacuum pressure forming, etc.
  • Multi-layer structure Bottles, cup-shaped containers, etc. obtained by stretch blow molding from (pipe etc.)
  • the molded body obtained by these secondary processing methods can be preferably used as food containers such as deep-drawn containers, cup-shaped containers, and bottles.
  • the amount of the monocarboxylic acid contained in the resin composition from the molecular weight of the monocarboxylic acid used was obtained by subtracting the amount of acid derived from the phosphorus compound determined above from the amount of acid obtained and assuming that it was the equivalent of the amount of monocarboxylic acid. was quantified.
  • Criteria A Number of nuggets 10 or less / 0.1 m 2
  • B The number of bumps is 11 or more and less than 50 / 0.1 m 2
  • C 50 to less than 300 pieces / 0.1 m 2
  • D 300 or more pieces / 0.1 m 2
  • Sampling the single-layer film obtained after resuming screw rotation and counting gel-like spots (about 150 ⁇ m or more that can be confirmed with the naked eye) until the number of spots reaches 10 or less / 0.1 m 2 was evaluated according to the following criteria as an index corresponding to the increase in the appearance of streaky appearance over time.
  • Standard C is a border level that can withstand actual use.
  • HEDP 1-hydroxyethane-1,1-diphosphonic acid
  • sodium acetate is 0.84 g / L
  • acetic acid is 0.38 g / L
  • boric acid is 0.25 g / L.
  • hydrous EVOH pellets ethylene unit content (Et) 32 mol%, saponification degree (DS) 99.98 mol%) having a water content of 105 mass% were added to 92.4 L of an aqueous solution in which each component was dissolved in water. Then, the immersion was performed at 25 ° C. for 6 hours with occasional stirring.
  • the pellet after the immersion was subjected to centrifugal dehydration, and then dried in a hot air dryer at 80 ° C. for 3 hours and then at 120 ° C. for 24 hours to obtain a resin composition pellet.
  • a resin composition pellet contained 30 ppm of 1-hydroxyethane-1,1-diphosphonic acid, 200 ppm of sodium acetate as a metal salt, 200 ppm of acetic acid as a monocarboxylic acid, and 175 ppm of boric acid as a boron compound. It was.
  • Examples 2 to 17 and Comparative Examples 1 to 9> Except having changed the component mix
  • Table 2 shows the results of analysis and evaluation of the obtained pellets according to the above.
  • HEDP is 1-hydroxyethane-1,1-diphosphonic acid
  • NTMP is nitrotris (methylenephosphonic acid)
  • EDTMP is ethylenediaminetetrakis (methylenephosphonic acid) hydrate. .
  • Examples 18 to 20> By operating in the same manner as in Example 1 except that the types of hydrous EVOH pellets used (Et of EVOH), the components blended in the aqueous solution, and the concentrations thereof were changed as shown in Table 1, pellets of the resin composition were obtained. Obtained. Table 2 shows the results of analysis and evaluation of the obtained pellets according to the above.
  • the resin composition contains a specific phosphorus compound and a metal salt in a specific amount, it becomes a determination of C or more in all evaluation items, and the color resistance and the time-dependent increase in the thickness It was possible to obtain a resin composition having excellent long-run properties such as suppression of corrosion. Moreover, the said characteristic was further improved by containing monocarboxylic acid and boric acid in a predetermined quantity.
  • Example 21> Except having changed the component mix
  • Table 4 shows the results of analyzing the obtained pellets according to the above.
  • appearance characteristics whether or not yellowing of the film end face occurred
  • Colorability evaluation during repeated reuse No coloration was observed, and the determination was A.
  • Examples 22 to 31 and Comparative Examples 10 to 18> Except having changed the component mix
  • Table 4 shows the results of analysis and evaluation of the obtained pellets according to the above.
  • Examples 32 to 34 The pellets of the resin composition were prepared by operating in the same manner as in Example 21 except that the types of hydrous EVOH pellets used (Et of EVOH) and the components and concentrations thereof contained in the aqueous solution were changed as shown in Table 3. Obtained. Table 4 shows the results of analysis and evaluation of the obtained pellets according to the above.
  • the resin composition contains a specific phosphorus compound and a metal salt in a predetermined amount, it becomes a determination of C or more in all evaluation items, and in coloration resistance and long-time molding In addition, it was possible to obtain a resin composition excellent in long run properties such that fish eyes and streaks are not generated. Moreover, the said characteristic was further improved by containing monocarboxylic acid and boric acid in a predetermined quantity.

Abstract

Provided are: a resin composition that has excellent appearance properties and long-run properties when being melted and molded, and that can inhibit the occurrence of yellowing even after being repeatedly re-used; and a molded article obtained using such a composition. The resin composition according to the present invention contains EVOH as a major ingredient, and is characterized in that the resin composition contains a phosphorus compound and a metal salt, the phosphorus compound is a condensed phosphoric acid, a compound having two or more phosphonic acid groups, or a combination thereof, the contained amount of the phosphorus compound is not less than 0.1 ppm but less than 50 ppm, the contained amount of the metal salt is 5-500 ppm in terms of the elemental metal. The metal salt is preferably an alkali metal salt, an alkaline-earth metal salt, or a combination thereof. The molded article according to the present invention has a portion formed of the resin composition.

Description

樹脂組成物及び成形体Resin composition and molded body
 本発明は、樹脂組成物及び成形体に関する。 The present invention relates to a resin composition and a molded body.
 エチレン-ビニルアルコール共重合体(以下、EVOHと略記する。)は、その優れた酸素遮断性等の性質から、フィルム、シート、容器などの各種包装材として広く用いられている。これらの包装材は、通常、溶融成形法により成形され、EVOHには、外観特性(黄変等の着色が少ないこと)に優れること、及び溶融成形時のロングラン性に優れることなどが求められる。 An ethylene-vinyl alcohol copolymer (hereinafter abbreviated as EVOH) is widely used as various packaging materials for films, sheets, containers, and the like because of its excellent oxygen barrier properties. These packaging materials are usually molded by a melt molding method, and EVOH is required to have excellent appearance characteristics (low coloration such as yellowing) and excellent long-run property during melt molding.
 包装材は多層構造体として構成されることが多いが、多層構造体の層間接着性等を高めるために、EVOH中に金属イオンを含有させたEVOH樹脂組成物とすることがある。しかし、EVOH中に金属イオンを含有させると着色が生じやすくなり、成形体の外観特性が低下するという不都合が生じる。 The packaging material is often configured as a multilayer structure, but may be an EVOH resin composition containing metal ions in EVOH in order to improve interlayer adhesion of the multilayer structure. However, when metal ions are contained in EVOH, coloring tends to occur, resulting in a disadvantage that the appearance characteristics of the molded body are deteriorated.
 また、通常、成形体を製品化する際に余分なシート端部(トリム)をカットするといったことが行われ、このトリムは有効利用する目的で回収して再利用される。しかし、この場合、EVOHが繰り返し熱履歴を受けることで熱劣化し、黄変等の着色が生じて成形体の外観特性が悪化するといった不都合が発生する。このため、再利用時の繰り返し熱履歴を受けても外観特性が悪化しないEVOH樹脂組成物が求められている。 Also, usually, when a molded product is commercialized, an extra sheet end (trim) is cut, and this trim is collected and reused for the purpose of effective use. However, in this case, EVOH undergoes repeated heat histories, causing thermal degradation, causing inconveniences such as yellowing or other coloring and deterioration of the appearance characteristics of the molded body. For this reason, there is a need for EVOH resin compositions that do not deteriorate in appearance characteristics even when subjected to repeated heat history during reuse.
 また、EVOHはその分子構造中に反応性の高い水酸基を多数有している。このため、EVOHは、溶融成形を長時間継続して運転した際に、ゲルやブツといった欠点が経時的に増加したり、スジ状の外観不良が経時的に増加して成形体としての商品価値が低下するといった、ロングラン性に係る課題を有する。なお、このようなゲルやブツなどの増加や、スジ状の外観不良の発生といったロングラン性の問題については、成形加工に用いる設備や運転条件によっていずれの問題が発生するかが異なり、両方の問題が発生する場合もある。いずれにせよ、長時間の連続運転においてもこのような経時的な変化の少ないロングラン性に優れたEVOH樹脂組成物が望まれている。 EVOH has a large number of highly reactive hydroxyl groups in its molecular structure. For this reason, when EVOH is operated continuously for a long time, defects such as gels and blisters increase over time, and streaky appearance defects increase over time, resulting in commercial value as a molded product. Has a problem related to long-run properties such as a decrease in In addition, about long run problems such as the increase in gels and blisters and the appearance of streaky appearance, which problem occurs depends on the equipment and operating conditions used for molding, both problems May occur. In any case, such an EVOH resin composition excellent in long run properties with little change with time even in continuous operation for a long time is desired.
 EVOHに要求されている上述の諸特性を向上させるために、特開昭64-66262号公報には、カルボン酸等の酸と金属イオンとを含有するEVOH樹脂組成物が記載されている。また、特許第5619874号公報には、多価カルボン酸と金属イオンとを含有するEVOH樹脂組成物が記載されている。これらのEVOH樹脂組成物は、外観特性及びロングラン性に優れているとされている。 In order to improve the above-mentioned various properties required for EVOH, JP-A-64-66262 discloses an EVOH resin composition containing an acid such as a carboxylic acid and a metal ion. Japanese Patent No. 5619874 describes an EVOH resin composition containing a polyvalent carboxylic acid and a metal ion. These EVOH resin compositions are said to be excellent in appearance characteristics and long run properties.
 しかしながら、色相や外観特性といった成形体の品質に対する要求は近年ますます高まってきており、従来の上記EVOH樹脂組成物によっても、近年ますます高まってきている色相や外観特性(ゲル、ブツ、ストリーク等)への要求品質に対しては十分に応えられていないのが実情である。また、トリムの再利用は環境配慮の観点から重要性が増してきているが、前述した繰り返し熱履歴を受けることによる黄変等の発生による外観特性の悪化に対しては有効な対策がないのが実情である。 However, demands on the quality of molded products such as hue and appearance characteristics have been increasing in recent years. Even with the above-mentioned EVOH resin composition, hue and appearance characteristics (gels, butts, streaks, etc.) have been increasing in recent years. The actual situation is that the quality required for) is not fully met. Reuse of trim is becoming more important from the viewpoint of environmental considerations, but there is no effective measure against deterioration of appearance characteristics due to occurrence of yellowing due to repeated heat history as described above. Is the actual situation.
特開昭64-66262号公報JP-A 64-66262 特許第5619874号公報Japanese Patent No. 5619874
 本発明は上述のような事情に基づいてなされたものであり、溶融成形における優れた外観特性やロングラン性を備え、特に再利用を繰り返した後においても黄変の発生を抑制することができる樹脂組成物、及びこのような組成物を用いて得られる成形体を提供することを目的とする。 The present invention has been made on the basis of the circumstances as described above, and has excellent appearance characteristics and long run properties in melt molding, and can suppress the occurrence of yellowing even after repeated reuse. It aims at providing the composition and the molded object obtained using such a composition.
 上記課題を解決するためになされた発明は、EVOHを主成分とする樹脂組成物であって、リン化合物及び金属塩を含有し、上記リン化合物が、縮合リン酸、2つ以上のホスホン酸基を有する化合物又はこれらの組み合わせであり、上記リン化合物の含有量が0.1ppm以上50ppm未満であり、上記金属塩の含有量が金属元素換算で5ppm以上500ppm以下であることを特徴とする。 The invention made in order to solve the above problems is a resin composition containing EVOH as a main component, containing a phosphorus compound and a metal salt, wherein the phosphorus compound is condensed phosphoric acid, two or more phosphonic acid groups Or a combination thereof, wherein the phosphorus compound content is 0.1 ppm or more and less than 50 ppm, and the metal salt content is 5 ppm or more and 500 ppm or less in terms of metal element.
 当該樹脂組成物は、縮合リン酸、2つ以上のホスホン酸基を有する化合物又はこれらの組み合わせである特定のリン化合物の含有量を上記範囲としていることで、黄変等の原因とされている金属イオンに対してリン酸基又はホスホン酸基が安定して配位し、金属イオンを取り込むことができると考えられる。すなわち、このように金属イオンが配位された状態で安定して存在することで、金属イオンが有するEVOHの黄変等の反応に対する触媒機能を抑制することができ、その結果、再利用を繰り返した場合においても黄変等の着色の発生を抑えることができる。また、当該樹脂組成物は、上記範囲の金属塩を含有しているため、長時間の成形においてもゲルやブツといった欠点が経時的に増大しない、あるいは長時間の成形においてもスジ状の外観不良が経時的に増大しないといった優れたロングラン性を発揮することができる。 The resin composition is considered to cause yellowing or the like by setting the content of a specific phosphorous compound that is condensed phosphoric acid, a compound having two or more phosphonic acid groups, or a combination thereof in the above range. It is considered that a phosphate group or a phosphonic acid group is stably coordinated with a metal ion and can incorporate the metal ion. That is, the presence of metal ions in a coordinated state in this manner can suppress the catalytic function for reactions such as yellowing of EVOH possessed by metal ions, and as a result, repeated reuse. Even in such a case, the occurrence of coloring such as yellowing can be suppressed. In addition, since the resin composition contains a metal salt in the above range, defects such as gels and blisters do not increase over time even during long-time molding, or streaky appearance defects even during long-time molding. Can exhibit an excellent long-run property such that does not increase with time.
 上記金属塩がアルカリ金属塩、アルカリ土類金属塩又はこれらの組み合わせであることが好ましい。上記金属塩がアルカリ金属塩であることが好ましい。アルカリ金属塩は、特に、長時間の成形においてもゲルやブツといった欠点が経時的に増大しないといったロングラン性を好適に発揮することができる。上記金属塩がアルカリ土類金属塩であり、上記アルカリ土類金属塩の含有量が金属元素換算で5ppm以上100ppm以下であることも好ましい。アルカリ土類金属塩は、特に、長時間の成形においてもスジ状の外観不良が経時的に増大しないといったロングラン性を好適に発揮することができる。 The metal salt is preferably an alkali metal salt, an alkaline earth metal salt, or a combination thereof. The metal salt is preferably an alkali metal salt. In particular, the alkali metal salt can suitably exhibit a long run property such that defects such as gels and blisters do not increase with time even during long-time molding. It is also preferable that the metal salt is an alkaline earth metal salt, and the content of the alkaline earth metal salt is 5 ppm or more and 100 ppm or less in terms of metal element. In particular, the alkaline earth metal salt can exhibit a long run property such that a streak-like appearance defect does not increase with time even in a long-time molding.
 当該樹脂組成物は、モノカルボン酸をさらに含有し、上記モノカルボン酸の含有量が5ppm以上500ppm以下であることが好ましい。また、当該樹脂組成物は、ホウ素化合物をさらに含有し、上記ホウ素化合物の含有量がホウ素元素換算で5ppm以上2,000ppm以下であることが好ましい。 The resin composition further contains a monocarboxylic acid, and the content of the monocarboxylic acid is preferably 5 ppm or more and 500 ppm or less. Moreover, the said resin composition contains a boron compound further, and it is preferable that content of the said boron compound is 5 ppm or more and 2,000 ppm or less in conversion of a boron element.
 本発明の成形体は、当該樹脂組成物から形成される部分を有する成形体である。当該成形体は、上述のように外観特性及びロングラン性に優れた樹脂組成物から得られる部分を備えるため、黄変等の着色、ゲル、ブツ、フィッシュアイ、スジ等の発生が抑制された優れた外観を有している。 The molded product of the present invention is a molded product having a part formed from the resin composition. Since the molded body is provided with a portion obtained from the resin composition having excellent appearance characteristics and long run properties as described above, the occurrence of coloring such as yellowing, gel, butts, fish eyes, and streaks is suppressed. It has a good appearance.
 本発明によれば、溶融成形における優れた外観特性やロングラン性を備え、特に再利用を繰り返した後においても黄変の発生を抑制することができる樹脂組成物、及びこのような組成物を用いて得られる成形体を提供することができる。 According to the present invention, a resin composition having excellent appearance characteristics and long run property in melt molding, and particularly capable of suppressing the occurrence of yellowing even after repeated reuse, and such a composition are used. It is possible to provide a molded product obtained in this way.
 以下、本発明の実施の形態について、樹脂組成物及び成形体の順に詳説する。 Hereinafter, embodiments of the present invention will be described in detail in the order of the resin composition and the molded body.
[樹脂組成物]
 本発明の樹脂組成物は、EVOHを主成分とし、リン化合物及び金属塩を含有する。なお、主成分とは、質量基準で最も含有量の多い成分をいう。
[Resin composition]
The resin composition of the present invention contains EVOH as a main component and a phosphorus compound and a metal salt. In addition, a main component means a component with most content on a mass basis.
(EVOH)
 EVOHは、エチレン単位及びビニルアルコール単位を有する共重合体である。但し、このEVOHは、他の構造単位を1種又は複数種含んでいてもよい。
(EVOH)
EVOH is a copolymer having ethylene units and vinyl alcohol units. However, this EVOH may contain one or more other structural units.
 EVOHは、公知の方法にて製造することができる。EVOHのエチレン単位含有量の下限としては15mol%が好ましく、20mol%がより好ましく、25mol%がさらに好ましい。一方、EVOHのエチレン単位含有量の上限としては60mol%が好ましく、55mol%がより好ましく、50mol%がさらに好ましい。EVOHのエチレン単位含有量を上記範囲とすることで、溶融成形後の黄変が抑制されると共に、ロングラン性により優れた樹脂組成物が得られる。EVOHのエチレン単位含有量が上記下限より小さいと、樹脂組成物のロングラン性や、得られる成形体の耐水性、耐熱水性及び高湿度下でのガスバリア性などが低下するおそれがある。逆に、EVOHのエチレン単位含有量が上記上限を超えると、得られる成形体のガスバリア性などが低下するおそれがある。 EVOH can be produced by a known method. As a minimum of ethylene unit content of EVOH, 15 mol% is preferred, 20 mol% is more preferred, and 25 mol% is still more preferred. On the other hand, the upper limit of the ethylene unit content of EVOH is preferably 60 mol%, more preferably 55 mol%, and even more preferably 50 mol%. By setting the ethylene unit content of EVOH within the above range, yellowing after melt molding is suppressed, and a resin composition that is more excellent in long run properties is obtained. If the ethylene unit content of EVOH is smaller than the above lower limit, the long-run property of the resin composition, the water resistance, hot water resistance and gas barrier property under high humidity of the resulting molded product may be deteriorated. On the other hand, when the ethylene unit content of EVOH exceeds the above upper limit, the gas barrier property and the like of the resulting molded article may be lowered.
 EVOHのけん化度の下限としては、80mol%が好ましく、95mol%がより好ましく、99mol%がさらに好ましい。EVOHのけん化度が上記下限より小さいと、得られる成形体のガスバリア性や外観特性が低下するおそれがある。 The lower limit of the saponification degree of EVOH is preferably 80 mol%, more preferably 95 mol%, and even more preferably 99 mol%. If the saponification degree of EVOH is smaller than the above lower limit, the gas barrier properties and appearance characteristics of the obtained molded product may be deteriorated.
 以下にEVOHの製造方法を具体的に説明する。EVOHは、通常、エチレンとビニルエステルとを共重合して得られるエチレン-ビニルエステル共重合体をけん化することで得られる。エチレンとビニルエステルとの重合は、溶液重合、懸濁重合、乳化重合、バルク重合等といった公知のいずれの方法によっても良く、また連続式及び回分式のいずれであってもよい。例えば、溶液重合の場合の重合条件は次の通りである。 The EVOH production method will be specifically described below. EVOH is usually obtained by saponifying an ethylene-vinyl ester copolymer obtained by copolymerizing ethylene and a vinyl ester. The polymerization of ethylene and vinyl ester may be carried out by any known method such as solution polymerization, suspension polymerization, emulsion polymerization, bulk polymerization, etc., and may be either continuous type or batch type. For example, the polymerization conditions in the case of solution polymerization are as follows.
 溶媒:アルコール類が好ましいが、その他エチレン、ビニルエステル及びエチレン-ビニルエステル共重合体を溶解し得る有機溶媒(ジメチルスルホキシドなど)を用いることができる。アルコール類としては、メチルアルコール、エチルアルコール、プロピルアルコール、n-ブチルアルコール、t-ブチルアルコール等を用いることができ、特にメチルアルコールが好ましい。 Solvent: Alcohols are preferable, but other organic solvents (such as dimethyl sulfoxide) that can dissolve ethylene, vinyl ester, and ethylene-vinyl ester copolymer can be used. As alcohols, methyl alcohol, ethyl alcohol, propyl alcohol, n-butyl alcohol, t-butyl alcohol and the like can be used, and methyl alcohol is particularly preferable.
 重合開始剤:2,2’-アゾビスイソブチロニトリル、2,2’-アゾビス-(2,4-ジメチルバレロニトリル)、2,2’-アゾビス-(4-メトキシ-2,4-ジメチルバレロニトリル)、2,2’-アゾビス-(2-シクロプロピルプロピオニトリル)等のアゾニトリル系開始剤、イソブチリルパーオキサイド、クミルパーオキシネオデカノエート、ジイソプロピルパーオキシカーボネート、ジ-n-プロピルパーオキシジカーボネート、ジシクロヘキシルパーオキシジカーボネート、t-ブチルパーオキシネオデカノエート、ラウロイルパーオキサイド、ベンゾイルパーオキサイド、t-ブチルハイドロパーオキサイド、ジアセチルパーオキサイド等の有機過酸化物系開始剤などを用いることができる。 Polymerization initiator: 2,2'-azobisisobutyronitrile, 2,2'-azobis- (2,4-dimethylvaleronitrile), 2,2'-azobis- (4-methoxy-2,4-dimethyl) Valeronitrile), azonitrile initiators such as 2,2′-azobis- (2-cyclopropylpropionitrile), isobutyryl peroxide, cumylperoxyneodecanoate, diisopropylperoxycarbonate, di-n-propyl Organic peroxide initiators such as peroxydicarbonate, dicyclohexylperoxydicarbonate, t-butylperoxyneodecanoate, lauroyl peroxide, benzoyl peroxide, t-butyl hydroperoxide, diacetyl peroxide, etc. Can be used.
 温度:20℃以上90℃以下、好ましくは40℃以上70℃以下。
 時間:2時間以上15時間以下、好ましくは3時間以上11時間以下。
 重合率:仕込みビニルエステルに対して10%以上90%以下、好ましくは30%以上80%以下。
 重合後の溶液中の樹脂分:5%以上85%以下、好ましくは20%以上70%以下。
Temperature: 20 ° C. or higher and 90 ° C. or lower, preferably 40 ° C. or higher and 70 ° C. or lower.
Time: 2 hours to 15 hours, preferably 3 hours to 11 hours.
Polymerization rate: 10% to 90%, preferably 30% to 80% with respect to the charged vinyl ester.
Resin content in the solution after polymerization: 5% to 85%, preferably 20% to 70%.
 重合に用いられる代表的なビニルエステルとしては、酢酸ビニルが挙げられるが、その他の脂肪族ビニルエステル、例えばギ酸ビニル、プロピオン酸ビニル、酪酸ビニル、イソ酪酸ビニル、ピバリン酸ビニル、バーサチック酸ビニル、カプロン酸ビニルなどが例示される。 Typical vinyl esters used for polymerization include vinyl acetate, but other aliphatic vinyl esters such as vinyl formate, vinyl propionate, vinyl butyrate, vinyl isobutyrate, vinyl pivalate, vinyl versatate, capron. Examples include vinyl acid.
 他にも、本発明の効果が阻害されない範囲であれば、共重合し得る他のエチレン性不飽和単量体を少量共重合させることができる。このようなエチレン性不飽和単量体としては、例えば
 プロピレン、n-ブテン、イソブチレン、1-ヘキセンなどのα-オレフィン類;
 3,4-ジアセトキシ-1-ブテンなどの1,2-ジエステル基を有する不飽和単量体;
 2-メチレン-1,3-プロパンジオールジアセテート(1,3-ジアセトキシ-2-メチレンプロパン)、2-メチレン-1,3-プロパンジオールジプロピオネート、2-メチレン-1,3-プロパンジオールジブチレートなどの1,3-ジエステル基を有する不飽和単量体;
 アクリル酸及びその塩;
 アクリル酸エステル基を有する不飽和単量体;
 メタクリル酸及びその塩;
 メタクリル酸エステル基を有する不飽和単量体;
 アクリルアミド、N-メチルアクリルアミド、N-エチルアクリルアミド、N,N-ジメチルアクリルアミド、ジアセトンアクリルアミド、アクリルアミドプロパンスルホン酸及びその塩、アクリルアミドプロピルジメチルアミン及びその塩(例えば4級塩);
 メタクリルアミド、N-メチルメタクリルアミド、N-エチルメタクリルアミド、メタクリルアミドプロパンスルホン酸及びその塩、メタクリルアミドプロピルジメチルアミン及びその塩(例えば4級塩);
 メチルビニルエーテル、エチルビニルエーテル、n-プロピルビニルエーテル、i-プロピルビニルエーテル、n-ブチルビニルエーテル、i-ブチルビニルエーテル、t-ブチルビニルエーテル、ドデシルビニルエーテル、ステアリルビニルエーテル、2,3-ジアセトキシ-1-ビニルオキシプロパンなどのビニルエーテル類;
 アクリロニトリル、メタクリロニトリルなどのシアン化ビニル類;塩化ビニル、フッ化ビニルなどのハロゲン化ビニル類;
 塩化ビニリデン、フッ化ビニリデンなどのハロゲン化ビニリデン類;
 酢酸アリル、2,3-ジアセトキシ-1-アリルオキシプロパン、塩化アリルなどのアリル化合物;
 マレイン酸、イタコン酸、フマル酸などの不飽和ジカルボン酸及びその塩又はそのエステル;
 ビニルトリメトキシシランなどのビニルシラン化合物;
 酢酸イソプロペニルなどが挙げられる。
In addition, other ethylenically unsaturated monomers that can be copolymerized can be copolymerized in a small amount as long as the effects of the present invention are not inhibited. Examples of such ethylenically unsaturated monomers include α-olefins such as propylene, n-butene, isobutylene and 1-hexene;
Unsaturated monomers having 1,2-diester groups such as 3,4-diacetoxy-1-butene;
2-methylene-1,3-propanediol diacetate (1,3-diacetoxy-2-methylenepropane), 2-methylene-1,3-propanediol dipropionate, 2-methylene-1,3-propanediol dibuty Unsaturated monomers having a 1,3-diester group such as a rate;
Acrylic acid and its salts;
An unsaturated monomer having an acrylate group;
Methacrylic acid and its salts;
An unsaturated monomer having a methacrylate group;
Acrylamide, N-methyl acrylamide, N-ethyl acrylamide, N, N-dimethyl acrylamide, diacetone acrylamide, acrylamide propane sulfonic acid and its salts, acrylamide propyl dimethylamine and its salts (eg quaternary salts);
Methacrylamide, N-methylmethacrylamide, N-ethylmethacrylamide, methacrylamidepropanesulfonic acid and salts thereof, methacrylamidepropyldimethylamine and salts thereof (eg quaternary salts);
Methyl vinyl ether, ethyl vinyl ether, n-propyl vinyl ether, i-propyl vinyl ether, n-butyl vinyl ether, i-butyl vinyl ether, t-butyl vinyl ether, dodecyl vinyl ether, stearyl vinyl ether, 2,3-diacetoxy-1-vinyloxypropane, etc. Vinyl ethers;
Vinyl cyanides such as acrylonitrile and methacrylonitrile; vinyl halides such as vinyl chloride and vinyl fluoride;
Vinylidene halides such as vinylidene chloride and vinylidene fluoride;
Allyl compounds such as allyl acetate, 2,3-diacetoxy-1-allyloxypropane, allyl chloride;
Unsaturated dicarboxylic acids such as maleic acid, itaconic acid, fumaric acid, and salts or esters thereof;
Vinylsilane compounds such as vinyltrimethoxysilane;
And isopropenyl acetate.
 所定時間の重合を行い所定の重合率に達した後、必要に応じて重合禁止剤を添加し、未反応のエチレンガスを蒸発除去した後、未反応のビニルエステルを除去する。エチレンを蒸発除去したエチレン-ビニルエステル共重合体から未反応のビニルエステルを除去する方法としては、例えば、ラシヒリングを充填した塔の上部から該共重合体溶液を一定速度で連続的に供給し、塔下部よりメタノール等の有機溶剤蒸気を吹き込み塔頂部よりメタノール等の有機溶剤と未反応ビニルエステルの混合蒸気を留出させ、塔底部より未反応ビニルエステルを除去したエチレン-ビニルエステル共重合体溶液を取り出す方法などが採用される。 After carrying out polymerization for a predetermined time to reach a predetermined polymerization rate, a polymerization inhibitor is added as necessary, and after removing unreacted ethylene gas, unreacted vinyl ester is removed. As a method for removing unreacted vinyl ester from the ethylene-vinyl ester copolymer from which ethylene has been removed by evaporation, for example, the copolymer solution is continuously supplied at a constant rate from the upper part of a column packed with Raschig rings, An ethylene-vinyl ester copolymer solution in which an organic solvent vapor such as methanol is blown from the bottom of the column, a mixed vapor of an organic solvent such as methanol and unreacted vinyl ester is distilled from the top of the column, and the unreacted vinyl ester is removed from the bottom of the column. The method of taking out is adopted.
 エチレン-ビニルエステル共重合体のけん化は、酸けん化やアルカリけん化といった公知の方法により行われる。例としてアルカリけん化を行う場合、上記で得られた未反応エチレン及び未反応ビニルエステルを除去した共重合体溶液にアルカリ触媒を添加し、共重合体中のビニルエステル部分をけん化する。けん化方法は連続式及び回分式のいずれも可能である。アルカリ触媒としては水酸化ナトリウム、水酸化カリウム、アルカリ金属アルコラートなどを用い、以下に示す条件が好適に用いられる。
 共重合体溶液濃度:10%以上50%以下。
 反応温度:30℃以上60℃以下。
 触媒使用量:0.02当量以上0.6当量以下(ビニルエステル成分当り)。
 時間:1時間6時間以下。
The saponification of the ethylene-vinyl ester copolymer is performed by a known method such as acid saponification or alkali saponification. For example, when alkali saponification is performed, an alkali catalyst is added to the copolymer solution from which the unreacted ethylene and unreacted vinyl ester obtained above are removed, and the vinyl ester portion in the copolymer is saponified. The saponification method can be either a continuous type or a batch type. As the alkali catalyst, sodium hydroxide, potassium hydroxide, alkali metal alcoholate or the like is used, and the following conditions are preferably used.
Copolymer solution concentration: 10% or more and 50% or less.
Reaction temperature: 30 ° C or higher and 60 ° C or lower.
Catalyst usage: 0.02 equivalents to 0.6 equivalents (per vinyl ester component).
Time: 1 hour 6 hours or less.
 このようにして得られたけん化反応後のEVOHは、けん化反応に用いた触媒の残渣や副生塩類、その他不純物等を含有するため、これらを必要に応じて中和、洗浄することにより除去することが好ましい。 The thus obtained EVOH after the saponification reaction contains catalyst residues, by-product salts, and other impurities used in the saponification reaction, and is removed by neutralization and washing as necessary. It is preferable.
 EVOHのメルトフローレート(JIS K 7210に準拠、温度210℃、荷重2160gでの測定値。以下、MFRと略記する。)の下限としては、0.1g/10分が好ましく、0.5g/10分がより好ましく、1g/10分がさらに好ましく、3g/10分が特に好ましい。一方、EVOHのMFRの上限としては、200g/10分が好ましく、50g/10分がより好ましく、30g/10分がさらに好ましく、15g/10分がよりさらに好ましく、10g/10分が特に好ましい。EVOHのMFRを上記範囲とすることで、溶融成形後の外観特性及びロングラン性に優れたものとなる。 The lower limit of the EVOH melt flow rate (according to JIS K 7210, temperature 210 ° C., load 2160 g, hereinafter abbreviated as MFR) is preferably 0.1 g / 10 minutes, preferably 0.5 g / 10. Minute is more preferable, 1 g / 10 minutes is further more preferable, and 3 g / 10 minutes is particularly preferable. On the other hand, the upper limit of MFR of EVOH is preferably 200 g / 10 minutes, more preferably 50 g / 10 minutes, further preferably 30 g / 10 minutes, still more preferably 15 g / 10 minutes, and particularly preferably 10 g / 10 minutes. By setting the MFR of EVOH in the above range, the appearance characteristics after melt molding and the long run property are excellent.
 当該樹脂組成物におけるEVOHの含有量の下限としては、例えば80質量%が好ましく、90質量%がより好ましい。さらに、EVOHの含有量の下限は、99質量%であってもよく、99.9質量%であってもよい。EVOHの含有量が上記下限以上であることにより、得られる成形体がEVOHの諸特性をより効果的に発揮することなどができる。なお、当該樹脂組成物中の各成分の含有量とは、乾燥した樹脂組成物全体に対する割合である(以下、同様)。 The lower limit of the EVOH content in the resin composition is, for example, preferably 80% by mass, and more preferably 90% by mass. Furthermore, 99 mass% may be sufficient as the minimum of content of EVOH, and 99.9 mass% may be sufficient as it. When the content of EVOH is equal to or more than the above lower limit, the obtained molded body can exhibit various characteristics of EVOH more effectively. In addition, content of each component in the said resin composition is a ratio with respect to the whole dried resin composition (hereinafter the same).
(リン化合物)
 当該樹脂組成物は、特定のリン化合物を含有する。このリン化合物は、縮合リン酸、2つ以上のホスホン酸基(-P(O)(OH))を有する化合物又はこれらの組み合わせである。すなわち、このリン化合物としては、1種の縮合リン酸や、2つ以上のホスホン酸基を有する化合物のみを用いてもよいし、複数種を組み合わせて用いてもよい。
(Phosphorus compound)
The resin composition contains a specific phosphorus compound. The phosphorus compound is condensed phosphoric acid, a compound having two or more phosphonic acid groups (—P (O) (OH) 2 ), or a combination thereof. That is, as this phosphorus compound, only one type of condensed phosphoric acid, a compound having two or more phosphonic acid groups may be used, or a plurality of types may be used in combination.
 当該樹脂組成物は、このようなリン化合物を含有することで、当該樹脂組成物を構成する他の成分の影響を受けることなく、溶融成形後及び再利用を繰り返した後においても黄変の発生を抑制することができる。縮合リン酸や、ホスホン酸基を2つ以上有するリン化合物は、黄変等の原因とされている金属イオンに対して安定して配位し、金属イオンを取り込むことができると考えられる。リン化合物が金属イオンに配位した状態で安定して存在することで、EVOHの分解や着色を触媒的に促進する金属イオンの作用を抑制していることが推測される。 By including such a phosphorus compound, the resin composition is not affected by other components constituting the resin composition, and yellowing occurs after melt molding and after repeated reuse. Can be suppressed. It is considered that a condensed phosphoric acid or a phosphorus compound having two or more phosphonic acid groups can stably coordinate to a metal ion that is responsible for yellowing or the like and take in the metal ion. It is presumed that the phosphorus compound is stably present in a coordinated state with the metal ion, thereby suppressing the action of the metal ion that catalytically promotes the decomposition and coloring of EVOH.
 縮合リン酸としては、例えばピロリン酸(二リン酸ともいう)、トリポリリン酸、テトラポリリン酸等が挙げられ、ピロリン酸が好ましい。2つ以上のホスホン酸基を有する化合物としては、例えばエチドロン酸(1-ヒドロキシエタン-1,1-ジホスホン酸ともいう)、アレンドロン酸、ニトロトリス(メチレンホスホン酸)、エチレンジアミンテトラ(メチレンホスホン酸)等を挙げることができ、これらの中でもエチドロン酸及びアレンドロン酸が好ましい。なお、縮合リン酸は、2つ以上のホスホン酸基を有していてもよいし、有していなくてもよい。また、2つ以上のホスホン酸基を有する化合物には、2つ以上のホスホン酸基を有する縮合リン酸が含まれていてもよい。一方、2つ以上のホスホン酸基を有する化合物は、2つ以上のホスホン酸基を有する縮合リン酸以外の化合物であってもよい。 Examples of condensed phosphoric acid include pyrophosphoric acid (also called diphosphoric acid), tripolyphosphoric acid, tetrapolyphosphoric acid, and the like, and pyrophosphoric acid is preferred. Examples of the compound having two or more phosphonic acid groups include etidronic acid (also referred to as 1-hydroxyethane-1,1-diphosphonic acid), alendronic acid, nitrotris (methylenephosphonic acid), ethylenediaminetetra (methylenephosphonic acid) Among them, etidronic acid and alendronic acid are preferable. In addition, the condensed phosphoric acid may or may not have two or more phosphonic acid groups. Further, the compound having two or more phosphonic acid groups may contain condensed phosphoric acid having two or more phosphonic acid groups. On the other hand, the compound having two or more phosphonic acid groups may be a compound other than condensed phosphoric acid having two or more phosphonic acid groups.
 これらのリン化合物は、酸素酸の状態で存在していてもよいし、金属イオンなどのカウンターカチオンと塩を形成したリン酸塩又はホスホン酸塩として存在していてもよい。また、水和物であってもよい。樹脂組成物中では、イオンとして解離していてもよいし、していなくてもよい。リン酸塩としては、第1リン酸塩、第2リン酸塩及び第3リン酸塩のいずれかの形でもよく、ホスホン酸塩としては、第1ホスホン酸塩及び第2ホスホン酸塩のいずれかの形でもよい。また、その対カチオン種としても特に限定されない。対カチオンの金属イオンと塩を形成したリン化合物を混合する場合、当該金属イオンは後述の金属塩中の金属イオンとしてもふるまう。 These phosphorus compounds may exist in the state of oxygen acid, or may exist as phosphates or phosphonates that form salts with counter cations such as metal ions. Moreover, a hydrate may be sufficient. In the resin composition, it may be dissociated as ions or not. As the phosphate, any of the first phosphate, the second phosphate and the third phosphate may be used. As the phosphonate, either the first phosphonate or the second phosphonate may be used. It may be in the form. Further, the counter cation species is not particularly limited. When a phosphorus compound that forms a salt with a metal ion of a counter cation is mixed, the metal ion also acts as a metal ion in a metal salt described later.
 このリン化合物の分子量としては特に制限されないが、上限としては例えば1,000が好ましく、600がより好ましい。一方、この下限としては、例えば170である。分子量が上記範囲の化合物であることにより、金属イオンへのより安定的な配位が可能となり、黄変の発生抑制能が高まる。 The molecular weight of this phosphorus compound is not particularly limited, but the upper limit is preferably 1,000, for example, and more preferably 600. On the other hand, the lower limit is 170, for example. By being a compound having a molecular weight within the above range, more stable coordination to a metal ion is possible, and the ability to suppress yellowing is increased.
 上記リン化合物が有するリン酸基(-O-P(O)(OH))及びホスホン酸基の数としては、2以上であるが、この上限としては、例えば6であり、4が好ましく、3がより好ましく、2がさらに好ましい。リン化合物が有するリン酸基及びホスホン酸基の数が上記範囲であることにより、金属イオンへのより安定的な配位が可能となり、黄変の発生抑制能が高まる。 The number of phosphoric acid groups (—O—P (O) (OH) 2 ) and phosphonic acid groups possessed by the phosphorus compound is 2 or more, and the upper limit is, for example, 6 and 4 is preferable, 3 is more preferable, and 2 is more preferable. When the number of the phosphoric acid group and the phosphonic acid group that the phosphorus compound has is within the above range, more stable coordination to the metal ion is possible, and the ability to suppress yellowing is increased.
 上記リン化合物の含有量の下限は、0.1ppmであり、0.5ppmが好ましく、3ppmがより好ましく、10ppmがさらに好ましく、20ppmが特に好ましい。リン化合物の含有量を上記下限以上とすることで、樹脂組成物自体の黄変等の着色を抑制することができるだけでなく、再利用を繰り返した後の成形体においても黄変の発生を抑制することができる。一方、このリン化合物の含有量は、50ppm未満であり、45ppm未満が好ましく、35ppm未満がより好ましい。リン化合物の含有量を上記上限未満とすることで、ロングラン性が優れた樹脂組成物とすることができる。 The lower limit of the content of the phosphorus compound is 0.1 ppm, preferably 0.5 ppm, more preferably 3 ppm, still more preferably 10 ppm, and particularly preferably 20 ppm. By setting the content of the phosphorus compound to the above lower limit or more, not only the coloring of the resin composition itself, such as yellowing, can be suppressed, but also the occurrence of yellowing can be suppressed in the molded product after repeated reuse. can do. On the other hand, the content of this phosphorus compound is less than 50 ppm, preferably less than 45 ppm, and more preferably less than 35 ppm. By making content of a phosphorus compound less than the said upper limit, it can be set as the resin composition excellent in long run property.
(金属塩)
 当該樹脂組成物は、金属塩を含有する。この金属塩としては、アルカリ金属塩、アルカリ土類金属塩、その他遷移金属塩などを挙げることができ、単独の金属種であっても良く、これらの複数の金属種からなるものであっても良い。上記金属塩としては、アルカリ金属塩、アルカリ土類金属塩又はこれらの組み合わせが好ましい。但し、この金属塩において、上記特定のリン化合物(縮合リン酸及びホスホン酸基を2つ以上有する化合物)の金属塩は含まれない。
(Metal salt)
The resin composition contains a metal salt. Examples of the metal salt include alkali metal salts, alkaline earth metal salts, and other transition metal salts, and may be a single metal species, or may be composed of a plurality of these metal species. good. As said metal salt, an alkali metal salt, alkaline-earth metal salt, or these combination is preferable. However, this metal salt does not include a metal salt of the specific phosphorus compound (a compound having two or more condensed phosphoric acid and phosphonic acid groups).
 上記金属塩の金属元素換算量の下限としては、樹脂組成物全体に対して5ppmであり、30ppmが好ましく、50ppmがより好ましく、100ppmであってもよい。一方、金属塩の金属元素換算量の上限としては、500ppmであり、400ppmが好ましく、300ppmがより好ましく、200ppmであってもよい。金属塩を上記範囲で含有することで、長時間の成形においてもゲルやブツといった欠点が経時的に増大しない、あるいは長時間の成形においてもスジ状の外観不良が経時的に増大しないといった優れたロングラン性と、黄変等の着色を抑制するといった優れた外観特性とのバランスがとれた樹脂組成物を得ることができる。 The lower limit of the metal element equivalent amount of the metal salt is 5 ppm, preferably 30 ppm, more preferably 50 ppm, and 100 ppm with respect to the entire resin composition. On the other hand, the upper limit of the metal element equivalent amount of the metal salt is 500 ppm, preferably 400 ppm, more preferably 300 ppm, and may be 200 ppm. By containing the metal salt in the above range, defects such as gels and blisters do not increase over time even during long-time molding, or streaky appearance defects do not increase over time even during long-time molding. It is possible to obtain a resin composition having a balance between long run properties and excellent appearance characteristics such as suppression of coloring such as yellowing.
 上記金属塩がアルカリ金属塩である樹脂組成物は、長時間の成形においてもゲルやブツといった欠点の発生の経時的な増加が抑制される点から好ましい。上記アルカリ金属塩を形成するアルカリ金属としては、リチウム、ナトリウム、カリウム等が挙げられるが、ナトリウム及びカリウムが好ましい。上記アルカリ金属塩としては、例えばリチウム、ナトリウム、カリウム等の脂肪族カルボン酸塩、芳香族カルボン酸塩、炭酸塩、塩酸塩、硝酸塩、硫酸塩、リン酸塩、金属錯体等が挙げられる。これらの中でも、酢酸ナトリウム、酢酸カリウム、炭酸ナトリウム、炭酸カリウム、リン酸ナトリウム及びリン酸カリウムが、入手容易である点などからより好ましい。 The resin composition in which the metal salt is an alkali metal salt is preferable in that an increase in generation of defects such as gels and bumps with time is suppressed even during long-time molding. Examples of the alkali metal that forms the alkali metal salt include lithium, sodium, and potassium, and sodium and potassium are preferable. Examples of the alkali metal salt include aliphatic carboxylates such as lithium, sodium, and potassium, aromatic carboxylates, carbonates, hydrochlorides, nitrates, sulfates, phosphates, metal complexes, and the like. Among these, sodium acetate, potassium acetate, sodium carbonate, potassium carbonate, sodium phosphate and potassium phosphate are more preferable because they are easily available.
 アルカリ金属塩の金属元素換算の含有量の下限としては、樹脂組成物全体に対して5ppmが好ましく、50ppmがより好ましく、100ppmがさらに好ましい。一方、アルカリ金属塩の金属元素換算の含有量の上限としては、500ppmであり、400ppmが好ましく、300ppmがより好ましい。アルカリ金属塩の含有量が上記下限以上であることで、EVOHの架橋を抑制し、長時間の成形においてもゲル・ブツの発生を抑制することができる。一方、アルカリ金属塩の含有量が上記上限以下であることで、黄変等の着色を抑制することができる。 The lower limit of the content of the alkali metal salt in terms of metal element is preferably 5 ppm, more preferably 50 ppm, and even more preferably 100 ppm with respect to the entire resin composition. On the other hand, the upper limit of the content of alkali metal salt in terms of metal element is 500 ppm, preferably 400 ppm, and more preferably 300 ppm. When the content of the alkali metal salt is not less than the above lower limit, EVOH cross-linking can be suppressed, and the generation of gels and blisters can be suppressed even during long-time molding. On the other hand, coloring, such as yellowing, can be suppressed because content of an alkali metal salt is below the said upper limit.
 金属塩が、アルカリ土類金属塩を含有する樹脂組成物は、長時間の成形においてもスジ状の外観不良の経時的な増加が抑制される点から好ましい。アルカリ土類金属塩としては、例えばベリリウム、マグネシウム、カルシウム、ストロンチウム、バリウム等の塩が挙げられる。工業的入手の点からはマグネシウムの塩及びカルシウムの塩であることが好ましく、脂肪族カルボン酸塩、芳香族カルボン酸塩、炭酸塩、塩酸塩、硝酸塩、硫酸塩、リン酸塩、金属錯体等が挙げられる。 A resin composition in which the metal salt contains an alkaline earth metal salt is preferable in that an increase in the appearance of streaky appearance over time is suppressed even during long-time molding. Examples of the alkaline earth metal salt include salts of beryllium, magnesium, calcium, strontium, barium and the like. Magnesium salts and calcium salts are preferred from the viewpoint of industrial availability, aliphatic carboxylates, aromatic carboxylates, carbonates, hydrochlorides, nitrates, sulfates, phosphates, metal complexes, etc. Is mentioned.
 アルカリ土類金属塩の金属元素換算の含有量の下限としては、樹脂組成物全体に対して5ppmが好ましく、30ppmがより好ましい。一方、アルカリ土類金属塩の金属元素換算の含有量の上限としては、150ppmであってもよいが、100ppmが好ましく、80ppmがより好ましい。アルカリ土類金属塩の含有量を上記下限以上とすることで、経時的なスジ状の外観不良の増大が効果的に抑制される。一方、アルカリ土類金属塩の含有量を上記上限以下とすることで黄変等の着色による外観特性の低下が効果的に抑制される。 The lower limit of the content of the alkaline earth metal salt in terms of metal element is preferably 5 ppm, more preferably 30 ppm, based on the entire resin composition. On the other hand, the upper limit of the content of the alkaline earth metal salt in terms of metal element may be 150 ppm, but is preferably 100 ppm, and more preferably 80 ppm. By setting the content of the alkaline earth metal salt to the above lower limit or more, an increase in the appearance of streak-like appearance over time is effectively suppressed. On the other hand, the fall of the external appearance characteristic by coloring, such as yellowing, is effectively suppressed by making content of alkaline-earth metal salt below the said upper limit.
 当該樹脂組成物における上記金属塩の含有量(金属元素換算)に対する上記リン化合物の含有量の比(リン化合物/金属塩)の下限としては、0.001が好ましく、0.005がより好ましく、0.01がさらに好ましく、0.05が特に好ましく、0.1がさらに特に好ましい。さらに、上記金属塩がアルカリ土類金属塩の場合などは、この比の下限は0.3がより好ましい。一方、この比の上限としては、例えば5が好ましく、1がより好ましい。さらに、上記金属塩がアルカリ金属塩の場合などは、この比の上限は0.5がより好ましく、0.3がさらに好ましい。金属塩とリン化合物の含有量の比を上記範囲とすることにより、本発明の作用効果をより効果的に発揮することができる。 The lower limit of the phosphorus compound content ratio (phosphorus compound / metal salt) to the metal salt content (in terms of metal element) in the resin composition is preferably 0.001, more preferably 0.005, 0.01 is more preferable, 0.05 is particularly preferable, and 0.1 is further particularly preferable. Further, when the metal salt is an alkaline earth metal salt, the lower limit of this ratio is more preferably 0.3. On the other hand, the upper limit of this ratio is preferably, for example, 5 and more preferably 1. Furthermore, when the metal salt is an alkali metal salt, the upper limit of this ratio is more preferably 0.5, and even more preferably 0.3. By setting the ratio of the content of the metal salt and the phosphorus compound within the above range, the effects of the present invention can be more effectively exhibited.
(モノカルボン酸)
 当該樹脂組成物は、モノカルボン酸を含有していてもよい。モノカルボン酸とは、分子内に1つのカルボキシ基を有する化合物である。
(Monocarboxylic acid)
The resin composition may contain a monocarboxylic acid. A monocarboxylic acid is a compound having one carboxy group in the molecule.
 モノカルボン酸の含有量は、臭気の低減の観点からは、樹脂組成物全体に対して500ppm以下であることが好ましく、300ppm以下であることがより好ましい。モノカルボン酸含量が上記上限以下であることで、樹脂組成物自体の臭気が低減されるのに加えて、樹脂組成物を溶融成形した際に発生する臭気が低減されることから、作業環境が改善される。また、溶融成形後の成形体の持つ臭気が低減されることから、当該樹脂組成物を用いた成形体は、米飯や飲料水といった特に臭気の発生が商品価値を損ねるような内容物に対しても、包装材として好ましく用いることができる。 The content of monocarboxylic acid is preferably 500 ppm or less, more preferably 300 ppm or less, based on the entire resin composition from the viewpoint of reducing odor. When the monocarboxylic acid content is not more than the above upper limit, the odor generated when the resin composition is melt-molded is reduced in addition to the odor of the resin composition itself, so that the working environment is reduced. Improved. In addition, since the odor of the molded article after melt molding is reduced, the molded article using the resin composition is particularly suitable for contents such as cooked rice and drinking water in which odor generation impairs the commercial value. Can also be preferably used as a packaging material.
 一方、モノカルボン酸の含有量は、品質安定性の観点からは、樹脂組成物全体に対して5ppm以上であることが好ましく、50ppm以上であることがより好ましい。モノカルボン酸の含有量が上記下限以上であることで、樹脂組成物の製造時に水溶液のpHの制御が容易となり、品質の安定した製品を得ることが容易となる。 On the other hand, the content of the monocarboxylic acid is preferably 5 ppm or more, more preferably 50 ppm or more with respect to the entire resin composition from the viewpoint of quality stability. When the content of the monocarboxylic acid is not less than the above lower limit, the pH of the aqueous solution can be easily controlled during the production of the resin composition, and it becomes easy to obtain a product with stable quality.
 モノカルボン酸としては、例えばギ酸、酢酸、プロピオン酸、酪酸、カプロン酸、カプリン酸、アクリル酸、メタクリル酸、安息香酸、2-ナフトエ酸を挙げることができる。これらの中でも、酢酸が好ましい。これらのモノカルボン酸は、ヒドロキシ基やハロゲン原子を有していてもよい。 Examples of the monocarboxylic acid include formic acid, acetic acid, propionic acid, butyric acid, caproic acid, capric acid, acrylic acid, methacrylic acid, benzoic acid, and 2-naphthoic acid. Among these, acetic acid is preferable. These monocarboxylic acids may have a hydroxy group or a halogen atom.
(ホウ素化合物)
 当該樹脂組成物は、ホウ素化合物を含有してもよい。ホウ素化合物としては、例えばホウ酸、ホウ酸エステル、ホウ酸塩、水素化ホウ素が挙げられる。具体的には、ホウ酸としては、例えばオルトホウ酸(HBO)、メタホウ酸、四ホウ酸が挙げられ、ホウ酸エステルとしては、例えばホウ酸トリエチル、ホウ酸トリメチルが挙げられ、ホウ酸塩としては、例えば上記の各種ホウ酸類のアルカリ金属塩、アルカリ土類金属塩、ホウ砂等が挙げられる。これらの中でもオルトホウ酸が好ましい。
(Boron compound)
The resin composition may contain a boron compound. Examples of the boron compound include boric acid, boric acid ester, borate, and borohydride. Specifically, examples of boric acid include orthoboric acid (H 3 BO 3 ), metaboric acid, and tetraboric acid. Examples of boric acid esters include triethyl borate and trimethyl borate. Examples of the salt include alkali metal salts, alkaline earth metal salts, borax and the like of the various boric acids described above. Of these, orthoboric acid is preferred.
 ホウ素化合物のホウ素元素換算の含有量の下限としては、樹脂組成物全体に対して5ppmが好ましく、10ppmがより好ましい。一方、ホウ素化合物のホウ素元素換算の含有量の上限としては、2,000ppmが好ましく、1,000ppmがより好ましく、500ppmがさらに好ましい。ホウ素化合物のホウ素元素換算の含有量が上記範囲であることで、樹脂組成物の溶融成形時の熱安定性を向上させることができ、その結果、成形加工時のロングラン性を更に優れたものとすることができる。詳細には、当該樹脂組成物にホウ素化合物が配合された場合、EVOHとホウ素化合物との間にキレート化合物が生成することで、樹脂組成物の熱安定性と機械的性質が向上すると考えられる。 The lower limit of the boron compound content of the boron compound is preferably 5 ppm, more preferably 10 ppm, based on the entire resin composition. On the other hand, the upper limit of the boron element content of the boron compound is preferably 2,000 ppm, more preferably 1,000 ppm, and even more preferably 500 ppm. When the boron compound content of the boron compound is in the above range, the thermal stability during melt molding of the resin composition can be improved, and as a result, the long run property during molding processing is further improved. can do. Specifically, when a boron compound is blended in the resin composition, it is considered that a chelate compound is generated between EVOH and the boron compound, thereby improving the thermal stability and mechanical properties of the resin composition.
(その他の添加剤等)
 当該樹脂組成物は、本発明の効果を損なわない範囲で、上述したEVOH、リン化合物、金属塩、モノカルボン酸及びホウ素化合物以外の他の成分を適量含んでいてもよい。このような他の成分としては、例えば可塑剤、安定剤、界面活性剤、色剤、紫外線吸収剤、スリップ剤、帯電防止剤、乾燥剤、架橋剤、充填剤、酸素吸収剤、各種繊維等の添加剤を挙げることができる。但し、これらの添加剤(EVOH、リン化合物、金属塩、モノカルボン酸及びホウ素化合物以外の成分)の樹脂組成物における含有量は、10質量%未満、1質量%未満、さらには0.1質量%未満とすることができる。
(Other additives)
The resin composition may contain an appropriate amount of components other than the above-described EVOH, phosphorus compound, metal salt, monocarboxylic acid, and boron compound as long as the effects of the present invention are not impaired. Examples of such other components include a plasticizer, a stabilizer, a surfactant, a colorant, an ultraviolet absorber, a slip agent, an antistatic agent, a drying agent, a crosslinking agent, a filler, an oxygen absorber, and various fibers. Can be mentioned. However, the content of these additives (components other than EVOH, phosphorus compound, metal salt, monocarboxylic acid and boron compound) in the resin composition is less than 10% by mass, less than 1% by mass, and further 0.1% by mass. %.
 また、当該樹脂組成物には、本発明の効果を損なわない範囲で、EVOH以外の熱可塑性樹脂を適量配合することも可能である。熱可塑性樹脂としては、例えば各種ポリオレフィン(ポリエチレン、ポリプロピレン、ポリ(1-ブテン)、ポリ(4-メチル-1-ペンテン)、エチレン-プロピレン共重合体、エチレンと炭素数4以上のα-オレフィンとの共重合体、オレフィンと無水マレイン酸との共重合体、エチレン-ビニルエステル共重合体、エチレン-アクリル酸エステル共重合体、又はこれらを不飽和カルボン酸若しくはその誘導体でグラフト変性した変性ポリオレフィンなど)、各種ナイロン(ナイロン6、ナイロン66、ナイロン6/66共重合体など)、ポリ塩化ビニル、ポリ塩化ビニリデン、ポリエステル、ポリスチレン、ポリアクリロニトリル、ポリウレタン、ポリアセタール、変性ポリビニルアルコール樹脂などが挙げられる。当該樹脂組成物がEVOH以外の熱可塑性樹脂を含有する場合、その配合量は50質量%未満が好ましく、30質量%未満がより好ましく、10質量%未満がさらに好ましく、1質量%未満がよりさらに好ましく、0.1質量%未満であってもよい。 In addition, an appropriate amount of a thermoplastic resin other than EVOH can be blended into the resin composition as long as the effects of the present invention are not impaired. Examples of the thermoplastic resin include various polyolefins (polyethylene, polypropylene, poly (1-butene), poly (4-methyl-1-pentene), ethylene-propylene copolymer, ethylene and α-olefin having 4 or more carbon atoms. Copolymer, copolymer of olefin and maleic anhydride, ethylene-vinyl ester copolymer, ethylene-acrylic ester copolymer, or modified polyolefin obtained by graft-modifying these with unsaturated carboxylic acid or derivatives thereof, etc. ), Various nylons (such as nylon 6, nylon 66, nylon 6/66 copolymer), polyvinyl chloride, polyvinylidene chloride, polyester, polystyrene, polyacrylonitrile, polyurethane, polyacetal, and modified polyvinyl alcohol resin. When the resin composition contains a thermoplastic resin other than EVOH, the blending amount is preferably less than 50% by mass, more preferably less than 30% by mass, further preferably less than 10% by mass, and even more preferably less than 1% by mass. Preferably, it may be less than 0.1% by mass.
 当該樹脂組成物のMFRの好ましい範囲は、EVOHの上述のMFRと同様であり、その範囲とすることにより得られる効果も、EVOHの場合と同様である。 The preferable range of MFR of the resin composition is the same as that of the above-mentioned MFR of EVOH, and the effect obtained by setting the range is the same as that of EVOH.
 当該樹脂組成物は、溶融成形によりペレット、フィルム、シート、容器、パイプ、繊維等、各種の成形体とすることができる。 The resin composition can be formed into various molded bodies such as pellets, films, sheets, containers, pipes and fibers by melt molding.
(樹脂組成物の製造方法)
 当該樹脂組成物は、例えばエチレンとビニルエステルとを共重合してエチレン-ビニルエステル共重合体を得る共重合工程(工程1)、及び上記エチレン-ビニルエステル共重合体をけん化してEVOHを得るけん化工程(工程2)を含み、上記共重合工程より後に上記エチレン-ビニルエステル共重合体又はEVOHと、上記リン化合物及び金属塩とを混合する混合工程(工程α)をさらに含む製造方法により効果的に得ることができる。なお、リン化合物及び金属塩は同時に混合してもよいし、別々にそれぞれ混合してもよい。以下、各工程について詳説する。
(Production method of resin composition)
The resin composition includes, for example, a copolymerization step (step 1) in which ethylene and vinyl ester are copolymerized to obtain an ethylene-vinyl ester copolymer, and EVOH is obtained by saponifying the ethylene-vinyl ester copolymer. The production method includes a saponification step (step 2), and further includes a mixing step (step α) of mixing the ethylene-vinyl ester copolymer or EVOH with the phosphorus compound and metal salt after the copolymerization step. Can be obtained. The phosphorus compound and the metal salt may be mixed simultaneously or separately. Hereinafter, each step will be described in detail.
(工程1:共重合工程)
 共重合工程は、エチレンとビニルエステルとの共重合の工程に加え、必要に応じて重合禁止剤を添加し、それに続いて未反応エチレン、未反応ビニルエステルを除去してエチレン-ビニルエステル共重合体溶液を得る工程を含む。エチレンとビニルエステルとの共重合方法としては、例えば溶液重合、懸濁重合、乳化重合、バルク重合などの公知の方法が挙げられる。具体的な重合条件等は、EVOHの製造方法として上述したとおりである。
(Step 1: Copolymerization step)
In the copolymerization step, in addition to the copolymerization step of ethylene and vinyl ester, a polymerization inhibitor is added as necessary, and then unreacted ethylene and unreacted vinyl ester are removed to remove ethylene-vinyl ester copolymer. Obtaining a coalesced solution. Examples of the copolymerization method of ethylene and vinyl ester include known methods such as solution polymerization, suspension polymerization, emulsion polymerization, and bulk polymerization. Specific polymerization conditions and the like are as described above for the EVOH production method.
(工程2:けん化工程)
 次に、エチレン-ビニルエステル共重合体溶液にアルカリ触媒等を添加し、溶液中の共重合体をけん化する。けん化の際の具体的条件等は、EVOHの製造方法として上述したとおりである。
(Process 2: Saponification process)
Next, an alkali catalyst or the like is added to the ethylene-vinyl ester copolymer solution to saponify the copolymer in the solution. Specific conditions and the like during saponification are as described above for the EVOH production method.
(工程α(1):混合工程)
 本混合工程では、共重合工程で得られたエチレン-ビニルエステル共重合体又はけん化工程で得られたEVOHと、上記リン化合物等とを混合する。但し、後述するように、EVOHの造粒後に混合工程を行うこともできる。この混合工程(工程α(1))として、例えば
(1)けん化工程に供するエチレン-ビニルエステル共重合体を含む溶液に予め上記リン化合物を添加する方法、
(2)けん化工程においてエチレン-ビニルエステル共重合体のけん化反応中に上記リン化合物を添加する方法、及び
(3)けん化工程でEVOHを得た後に上記リン化合物を混合する方法
を用いることができる。
(Process α (1): Mixing process)
In this mixing step, the ethylene-vinyl ester copolymer obtained in the copolymerization step or EVOH obtained in the saponification step is mixed with the phosphorus compound and the like. However, as will be described later, the mixing step can be performed after the granulation of EVOH. As this mixing step (step α (1)), for example, (1) a method of previously adding the phosphorus compound to a solution containing an ethylene-vinyl ester copolymer used for the saponification step,
(2) A method of adding the phosphorus compound during the saponification reaction of the ethylene-vinyl ester copolymer in the saponification step, and (3) a method of mixing the phosphorus compound after obtaining EVOH in the saponification step. .
(工程3:造粒工程)
 当該樹脂組成物をペレットの形状で得るには、共重合工程及びけん化工程の後に造粒工程を設ければよい。EVOHは、けん化反応に用いた溶媒を含む溶液の形で得られるため、溶液中に残存したアルカリ等の触媒や酢酸ナトリウム等の副生物を除去するために洗浄が行われる。この洗浄操作を容易にするために、けん化工程で得られたEVOH含有溶液を造粒して、EVOHの含水ペレットとすることが好ましい。
(Process 3: Granulation process)
In order to obtain the resin composition in the form of pellets, a granulation step may be provided after the copolymerization step and the saponification step. Since EVOH is obtained in the form of a solution containing the solvent used in the saponification reaction, washing is performed in order to remove a catalyst such as alkali and a by-product such as sodium acetate remaining in the solution. In order to facilitate this washing operation, it is preferable to granulate the EVOH-containing solution obtained in the saponification step into EVOH hydrous pellets.
 造粒の操作としては、例えば、(I)EVOH含有溶液を凝固浴に押出して、冷却固化させた後又は直後にカットする方法、(II)EVOHの溶液を水蒸気と接触させて予めEVOHの含水樹脂組成物としてカットする方法が挙げられる。これらの方法により得られたEVOHの含水ペレット中の含水率は、EVOHの乾燥質量基準で40質量%以上200質量%以下であることが好ましい。 As granulation operations, for example, (I) a method in which an EVOH-containing solution is extruded into a coagulation bath and is cooled and solidified or cut immediately after, or (II) the EVOH solution is brought into contact with water vapor in advance to contain EVOH-containing water. The method of cutting as a resin composition is mentioned. The moisture content of the EVOH hydrous pellets obtained by these methods is preferably 40% by mass or more and 200% by mass or less based on the dry mass of EVOH.
(工程4:乾燥工程)
 造粒工程で得られたEVOHの含水ペレットは、乾燥することでEVOHの乾燥ペレットとすることが好ましい。乾燥ペレット中の水分率は、成形加工時のボイドの発生といった成形トラブルを防ぐ目的から、乾燥ペレット全体に対して1.0質量%以下であることが好ましく、0.8質量%以下であることがより好ましく、0.5質量%以下であることがさらに好ましい。
(Process 4: Drying process)
The EVOH hydrous pellets obtained in the granulation step are preferably dried to form EVOH dry pellets. The moisture content in the dry pellets is preferably 1.0% by mass or less and 0.8% by mass or less with respect to the entire dry pellets for the purpose of preventing molding troubles such as generation of voids during molding. Is more preferably 0.5% by mass or less.
 含水ペレットの乾燥方法としては、例えば静置乾燥や流動乾燥が挙げられる。これらの乾燥方法は単独で用いてもよいし、複数を組み合わせて用いてもよい。乾燥処理は連続式及びバッチ式いずれの方法で行っても良い。また、複数の乾燥方式を組み合わせて行う場合は、各乾燥方式について連続式及びバッチ式を自由に選択できる。乾燥を低酸素濃度又は無酸素状態で行うことも、乾燥中の酸素による樹脂組成物の劣化を低減できる点で好ましい。 Examples of the method for drying the water-containing pellets include stationary drying and fluidized drying. These drying methods may be used alone or in combination. The drying treatment may be performed by either a continuous method or a batch method. Moreover, when performing combining several drying methods, a continuous type and a batch type can be freely selected about each drying method. It is also preferable to perform the drying at a low oxygen concentration or an oxygen-free state from the viewpoint that the deterioration of the resin composition due to oxygen during drying can be reduced.
(工程α(2):混合工程)
 混合工程は、造粒後に行ってもよい。造粒工程以降にリン化合物等の混合を行う方法としては、例えば
(1)EVOHの含水ペレットを上記リン化合物等を含有する溶液と接触させる方法、及び
(2)EVOHの含水ペレットと上記リン化合物等とを押出機内で溶融混練する方法
が挙げられる。この際、モノカルボン酸、アルカリ金属塩、アルカリ土類金属塩、ホウ素化合物等を同時にEVOHと混合することができる。
(Process α (2): Mixing process)
The mixing step may be performed after granulation. As a method of mixing a phosphorus compound or the like after the granulation step, for example, (1) a method of bringing a water-containing pellet of EVOH into contact with a solution containing the phosphorus compound or the like, and (2) a water-containing pellet of EVOH and the phosphorus compound And the like are melt kneaded in an extruder. At this time, monocarboxylic acid, alkali metal salt, alkaline earth metal salt, boron compound and the like can be mixed with EVOH at the same time.
 上記(1)のように浸漬する場合、含水ペレットの形状は任意であり、操作はバッチ方式及び連続方式のいずれの方法であってもよい。浸漬は、樹脂組成物に含有させる各成分をそれぞれ単独で溶解した複数の溶液に分けてもよく、複数の成分を溶解した液を用いて一度に処理してもよい。 When immersed as in (1) above, the shape of the water-containing pellet is arbitrary, and the operation may be either a batch method or a continuous method. The immersion may be divided into a plurality of solutions in which each component to be contained in the resin composition is individually dissolved, or may be processed at once using a solution in which a plurality of components are dissolved.
 なお、当該樹脂組成物の製造方法において、造粒工程と同時に混合工程を行ってもよい。すなわち、例えば造粒操作において、凝固浴に予め上記リン化合物及び金属塩を含有させればよい。 In addition, in the manufacturing method of the said resin composition, you may perform a mixing process simultaneously with a granulation process. That is, for example, in the granulation operation, the above phosphorus compound and metal salt may be previously contained in the coagulation bath.
[成形体]
 当該成形体は、当該樹脂組成物から形成される部分を有する成形体である。当該成形体は、当該樹脂組成物のみから形成されていてもよいし、当該EVOH樹脂から形成された部分を一部に有する例えば積層体等であってもよい。
[Molded body]
The said molded object is a molded object which has a part formed from the said resin composition. The said molded object may be formed only from the said resin composition, for example, a laminated body etc. which have a part formed from the said EVOH resin in part may be sufficient as it.
 当該成形体としては、ペレット、フィルム、シート、容器、パイプ、繊維等を挙げることができる。当該成形体は、通常、当該樹脂組成物の溶融成形により成形される。これらの成形体は再使用の目的で粉砕し再度成形することも可能である。また、フィルム、シート、繊維等を一軸又は二軸延伸することも可能である。溶融成形法としては、例えば押出成形、インフレーション押出、ブロー成形、溶融紡糸、射出成形等公知のいずれの成形法も適用可能である。 Examples of the molded body include pellets, films, sheets, containers, pipes, fibers, and the like. The molded body is usually molded by melt molding of the resin composition. These molded bodies can be pulverized and molded again for the purpose of reuse. It is also possible to uniaxially or biaxially stretch films, sheets, fibers, and the like. As the melt molding method, for example, any known molding method such as extrusion molding, inflation extrusion, blow molding, melt spinning, and injection molding can be applied.
 溶融成形の際の溶融温度としては、150℃以上300℃以下程度が好ましく、通常は200℃以上250℃以下程度の溶融温度が採用される。こうして得られた成形体は、溶融成形後の黄変等の着色が抑制されていると共に、ゲル、ブツ、フィッシュアイ、スジ等が抑制された優れた外観特性を有している。 The melting temperature at the time of melt molding is preferably about 150 ° C. or more and 300 ° C. or less, and usually a melting temperature of about 200 ° C. or more and 250 ° C. or less is employed. The molded body thus obtained has excellent appearance characteristics in which coloring such as yellowing after melt molding is suppressed and gel, butts, fish eyes, streaks and the like are suppressed.
 当該成形体は、当該樹脂組成物から得られる層を少なくとも一層備える多層構造体であってもよい。上記多層構造体は、外観特性やロングラン性に優れた樹脂組成物から得られる層を有しているため、黄変等の着色や、ゲル及びブツの発生又はフィッシュアイやスジ等が抑制された優れた外観特性を有している。 The molded body may be a multilayer structure including at least one layer obtained from the resin composition. Since the multilayer structure has a layer obtained from a resin composition having excellent appearance characteristics and long run properties, coloring such as yellowing, generation of gels and blisters, fish eyes and stripes are suppressed. Has excellent appearance characteristics.
 上記多層構造体の層構造としては、例えば、当該樹脂組成物から得られる層をE、接着性樹脂から得られる層をAd、熱可塑性樹脂から得られる層をTで表わした場合、T/E/T、E/Ad/T、T/Ad/E/Ad/Tといった構造が挙げられる。これらの各層は、単層であってもよいし、多層であってもよい。また、上記以外の他の層を含んでもよい。 As the layer structure of the multilayer structure, for example, when the layer obtained from the resin composition is represented by E, the layer obtained from the adhesive resin is represented by Ad, and the layer obtained from the thermoplastic resin is represented by T, T / E / T, E / Ad / T, and T / Ad / E / Ad / T. Each of these layers may be a single layer or a multilayer. Moreover, you may include other layers other than the above.
 上記接着性樹脂としては、例えばカルボン酸変性ポリオレフィンを含有する接着性樹脂が挙げられる。カルボン酸変性ポリオレフィンとしては、オレフィン系重合体にエチレン性不飽和カルボン酸、そのエステル又はその無水物を化学的(例えば付加反応、グラフト反応等)に結合させて得られるカルボキシル基を含有する変性オレフィン系重合体を好適に用いることができる。エチレン性不飽和カルボン酸、そのエステル又はその無水物としては、マレイン酸、フマル酸、イタコン酸、無水マレイン酸、無水イタコン酸、マレイン酸モノメチルエステル、マレイン酸モノエチルエステル、マレイン酸ジエチルエステル、フマル酸モノメチルエステル等が挙げられ、無水マレイン酸がより好ましい。これらの接着性樹脂は単独で用いてもよいし、また二種以上を混合して用いてもよい。 Examples of the adhesive resin include an adhesive resin containing a carboxylic acid-modified polyolefin. As the carboxylic acid-modified polyolefin, a modified olefin containing a carboxyl group obtained by chemically bonding an ethylenically unsaturated carboxylic acid, its ester or its anhydride to an olefin polymer (for example, addition reaction, graft reaction, etc.) A polymer can be preferably used. Examples of the ethylenically unsaturated carboxylic acid, its ester or its anhydride include maleic acid, fumaric acid, itaconic acid, maleic anhydride, itaconic anhydride, maleic acid monomethyl ester, maleic acid monoethyl ester, maleic acid diethyl ester, fumaric acid Acid monomethyl ester and the like, and maleic anhydride is more preferable. These adhesive resins may be used alone or in admixture of two or more.
 熱可塑性樹脂としては、例えば直鎖状低密度ポリエチレン、低密度ポリエチレン、中密度ポリエチレン、高密度ポリエチレン、エチレン-酢酸ビニル共重合体、エチレン-プロピレン共重合体、ポリプロピレン、プロピレン-α-オレフィン共重合体、ポリブテン、ポリペンテン等のオレフィンの単独又はその共重合体;ポリエチレンテレフタレート等のポリエステル;ポリエステルエラストマー;ナイロン6、ナイロン66等のポリアミド;ポリスチレン;ポリ塩化ビニル;ポリ塩化ビニリデン;アクリル系樹脂;ビニルエステル系樹脂;ポリウレタンエラストマー;ポリカーボネート;塩素化ポリエチレン;塩素化ポリプロピレンが挙げられる。これらの中でも、ポリプロピレン、ポリエチレン、エチレン-プロピレン共重合体、エチレン-酢酸ビニル共重合体、ポリアミド、ポリスチレン及びポリエステルが好ましく用いられる。 Examples of the thermoplastic resin include linear low density polyethylene, low density polyethylene, medium density polyethylene, high density polyethylene, ethylene-vinyl acetate copolymer, ethylene-propylene copolymer, polypropylene, propylene-α-olefin copolymer Polyolefins such as polymers, polybutenes, polypentenes or copolymers thereof; polyesters such as polyethylene terephthalate; polyester elastomers; polyamides such as nylon 6 and nylon 66; polystyrenes; polyvinyl chloride; polyvinylidene chloride; Resin, polyurethane elastomer, polycarbonate, chlorinated polyethylene, and chlorinated polypropylene. Among these, polypropylene, polyethylene, ethylene-propylene copolymer, ethylene-vinyl acetate copolymer, polyamide, polystyrene and polyester are preferably used.
 上記多層構造体を製造する方法としては、例えば以下の方法が挙げられる。
(1)当該樹脂組成物から得られる成形体上に熱可塑性樹脂を溶融押出する方法
(2)当該樹脂組成物と他の熱可塑性樹脂とを共押出する方法
(3)当該樹脂組成物と熱可塑性樹脂とを共射出する方法
(4)当該樹脂組成物から得られる成形体と他の基材とを接着剤を用いて積層する方法
Examples of the method for producing the multilayer structure include the following methods.
(1) Method of melt-extruding a thermoplastic resin on a molded body obtained from the resin composition (2) Method of co-extruding the resin composition and another thermoplastic resin (3) The resin composition and heat Method of co-injecting a plastic resin (4) Method of laminating a molded body obtained from the resin composition and another substrate using an adhesive
 これらの方法の中でも、(2)の方法を好ましく用いることができる。これは、本発明の樹脂組成物は、高温条件下で溶融してもロングラン性に優れ、かつ、その後の着色も抑制されているため、高融点の他の熱可塑性樹脂と共押出しても、着色が抑制されて外観特性に優れた多層構造体を得ることができるからである。共押出の方法としては、例えばマルチマニホールド合流方式Tダイ法、フィードプロック合流方式Tダイ法、インフレーション法等を挙げることができる。 Among these methods, the method (2) can be preferably used. This is because the resin composition of the present invention is excellent in long run properties even when melted under high temperature conditions, and subsequent coloring is also suppressed, so even if it is co-extruded with other thermoplastic resins having a high melting point, It is because coloring can be suppressed and a multilayer structure excellent in appearance characteristics can be obtained. Examples of the co-extrusion method include a multi-manifold joining method T-die method, a feed block joining method T-die method, and an inflation method.
 上述の共押出で得られた多層構造体を二次加工することで、例えば以下の成形体が得られる。
(1)多層構造体(シート又はフィルム等)を一軸又は二軸方向に延伸及び熱処理することにより得られる多層延伸シート又はフィルム
(2)多層構造体(シート又はフィルム等)を圧延することにより得られる多層圧延シート又はフィルム
(3)多層構造体(シート又はフィルム等)を真空成形、圧空成形、真空圧空成形等、熱成形加工することにより得られる多層トレー又はカップ状容器
(4)多層構造体(パイプ等)からのストレッチブロー成形等により得られるボトル、カップ状容器等
By subjecting the multilayer structure obtained by the above-described coextrusion to secondary processing, for example, the following molded body is obtained.
(1) A multilayer stretched sheet or film obtained by stretching and heat-treating a multilayer structure (sheet or film, etc.) in a uniaxial or biaxial direction. (2) Obtained by rolling a multilayer structure (sheet or film, etc.). Multi-layer rolled sheet or film (3) Multi-layer tray or cup-shaped container obtained by thermoforming a multi-layer structure (sheet or film, etc.) such as vacuum forming, pressure forming, vacuum pressure forming, etc. (4) Multi-layer structure Bottles, cup-shaped containers, etc. obtained by stretch blow molding from (pipe etc.)
 なお、上記以外の二次加工法を用いてもよい。これらの二次加工法により得られる成形体は、例えば深絞り容器、カップ状容器、ボトル等の食品容器として好ましく用いることができる。 Note that secondary processing methods other than those described above may be used. The molded body obtained by these secondary processing methods can be preferably used as food containers such as deep-drawn containers, cup-shaped containers, and bottles.
 以下、実施例によって本発明をさらに詳細に説明する。後述の実施例及び比較例において、分析及び評価は以下に示す方法にて行った。 Hereinafter, the present invention will be described in more detail with reference to examples. In Examples and Comparative Examples described later, analysis and evaluation were performed by the following methods.
(1)含水EVOHペレットの含水率の測定
 ハロゲン水分率分析装置を用い、乾燥温度180℃、乾燥時間20分、サンプル量10gの条件で含水EVOHペレットの含水率を、加熱乾燥重量測定法により測定した。以下に示す含水EVOHの含水率は、乾燥EVOH基準の質量%とする。
(1) Measurement of water content of water-containing EVOH pellets Using a halogen water content analyzer, the water content of water-containing EVOH pellets was measured by a thermodry weight measurement method under the conditions of a drying temperature of 180 ° C., a drying time of 20 minutes, and a sample amount of 10 g. did. The water content of the water-containing EVOH shown below is set to mass% based on the dry EVOH.
(2)リン化合物の定量
 樹脂組成物ペレット0.5gをテフロン(登録商標)製圧力容器に入れ、これに濃硝酸5mLを加えて室温で30分間分解させた。分解後に蓋をし、湿式分解装置(アクタック社の「MWS-2」)により150℃で10分間、次いで180℃で5分間加熱することでさらに分解を行い、その後室温まで冷却した。この処理液を50mLのメスフラスコ(TPX製)に移し、純水でメスアップして測定用試料溶液とした。この試料溶液について、ICP発光分光分析装置(パーキンエルマー社の「OPTIMA4300DV」)によりリン元素の含有量を求めた。リン元素含有量より、使用したリン化合物の分子量を用いてリン化合物の量を定量した。
(2) Determination of phosphorus compound 0.5 g of resin composition pellets were placed in a Teflon (registered trademark) pressure vessel, and 5 mL of concentrated nitric acid was added thereto and decomposed at room temperature for 30 minutes. After decomposition, the lid was covered, and further decomposition was carried out by heating at 150 ° C. for 10 minutes and then at 180 ° C. for 5 minutes by a wet decomposition apparatus (“ACTS Corporation” MWS-2), and then cooled to room temperature. This treatment liquid was transferred to a 50 mL volumetric flask (manufactured by TPX) and diluted with pure water to obtain a measurement sample solution. About this sample solution, content of the phosphorus element was calculated | required with the ICP emission-spectral-analysis apparatus ("OPTIMA4300DV" of Perkin Elmer). From the phosphorus element content, the amount of the phosphorus compound was quantified using the molecular weight of the phosphorus compound used.
(3)金属塩の定量
 樹脂組成物ペレット0.5gをテフロン(登録商標)製圧力容器に入れ、ここに濃硝酸5mLを加えて室温で30分間分解させた。分解後に蓋をし、湿式分解装置(アクタック社の「MWS-2」)により150℃で10分間、次いで180℃で5分間加熱することでさらに分解を行い、その後室温まで冷却した。この処理液を50mLのメスフラスコ(TPX製)に移し、純水でメスアップして測定用試料溶液とした。この試料溶液について、ICP発光分光分析装置(パーキンエルマー社の「OPTIMA4300DV」)により金属元素の含有量を求め、金属塩量を金属元素換算で定量した。
(3) Quantification of metal salt 0.5 g of resin composition pellets were placed in a pressure vessel made of Teflon (registered trademark), and 5 mL of concentrated nitric acid was added thereto and decomposed at room temperature for 30 minutes. After decomposition, the lid was covered, and further decomposition was carried out by heating at 150 ° C. for 10 minutes and then at 180 ° C. for 5 minutes by a wet decomposition apparatus (“ACTS Corporation” MWS-2), and then cooled to room temperature. This treatment liquid was transferred to a 50 mL volumetric flask (manufactured by TPX) and diluted with pure water to obtain a measurement sample solution. About this sample solution, content of the metal element was calculated | required with the ICP emission-spectral-analysis apparatus ("OPTIMA4300DV" of Perkin Elmer), and the amount of metal salts was quantified in conversion of the metal element.
(4)モノカルボン酸の定量
 樹脂組成物ペレットを凍結粉砕して得られたEVOH粉末10gとイオン交換水50mLとを100mL共栓付き三角フラスコに投入し、冷却コンデンサーを付け、95℃で10時間撹拌して抽出液を得た。得られた抽出液25mLに滴定用指示薬としてフェノールフタレイン2滴を加えたものについて、0.01mol/Lの水酸化ナトリウム溶液にて中和滴定し、酸量を算出した。得られた酸量から上記で定量したリン化合物由来の酸量を除いたものを、モノカルボン酸量の当量とし、用いたモノカルボン酸の分子量から樹脂組成物中に含まれるモノカルボン酸の量を定量した。
(4) Quantification of monocarboxylic acid 10 g of EVOH powder obtained by freeze-pulverizing the resin composition pellets and 50 mL of ion-exchanged water were put into a 100 mL conical flask with a stopper, attached with a cooling condenser, and at 95 ° C. for 10 hours. An extract was obtained by stirring. A solution obtained by adding 2 drops of phenolphthalein as a titration indicator to 25 mL of the obtained extract was subjected to neutralization titration with a 0.01 mol / L sodium hydroxide solution to calculate the acid amount. The amount of the monocarboxylic acid contained in the resin composition from the molecular weight of the monocarboxylic acid used was obtained by subtracting the amount of acid derived from the phosphorus compound determined above from the amount of acid obtained and assuming that it was the equivalent of the amount of monocarboxylic acid. Was quantified.
(5)ホウ素化合物の定量
 樹脂組成物ペレット0.5gをテフロン(登録商標)製圧力容器に入れ、ここに濃硝酸5mLを加えて室温で30分間分解させた。分解後に蓋をし、湿式分解装置(アクタック社の「MWS-2」)により150℃で10分間、次いで180℃で5分間加熱することでさらに分解を行い、その後室温まで冷却した。この処理液を50mLのメスフラスコ(TPX製)に移し純水でメスアップして測定用試料溶液とした。この試料溶液について、ICP発光分光分析装置(パーキンエルマー社の「OPTIMA4300DV」)によりホウ素化合物の量をホウ素元素換算で定量した。
(5) Quantitative determination of boron compound 0.5 g of resin composition pellets were placed in a pressure vessel made of Teflon (registered trademark), 5 mL of concentrated nitric acid was added thereto, and the mixture was decomposed at room temperature for 30 minutes. After decomposition, the lid was covered, and further decomposition was carried out by heating at 150 ° C. for 10 minutes and then at 180 ° C. for 5 minutes by a wet decomposition apparatus (“ACTS Corporation” MWS-2), and then cooled to room temperature. This treatment liquid was transferred to a 50 mL volumetric flask (manufactured by TPX) and diluted with pure water to obtain a measurement sample solution. With respect to this sample solution, the amount of the boron compound was quantified in terms of boron element using an ICP emission spectroscopic analyzer (“OPTIMA4300DV” manufactured by PerkinElmer).
(6)樹脂組成物を用いた単層フィルムの作製
 樹脂組成物ペレットを、東洋精機製作所社の20mm押出機「D2020」(D(mm)=20、L/D=20、圧縮比=2.0、スクリュー:フルフライト)を用いて単層製膜を以下の条件で行い、実施例及び比較例ごとに引取りロール速度を調整することで、20μmの単層フィルムを得た。
  押出温度:供給部/圧縮部/計量部/ダイ
       =170/210/210/210℃
  スクリュー回転数:40rpm
  引取りロール温度:80℃
(6) Production of single layer film using resin composition The resin composition pellets were produced by using a 20 mm extruder “D2020” (D (mm) = 20, L / D = 20, compression ratio = 2. (0, screw: full flight) was used to form a single layer under the following conditions, and a take-up roll speed was adjusted for each of Examples and Comparative Examples to obtain a 20 μm single layer film.
Extrusion temperature: supply unit / compression unit / metering unit / die = 170/210/210/210 ° C.
Screw rotation speed: 40rpm
Take-up roll temperature: 80 ° C
(7)外観特性(フィルム端面の黄変の発生の有無)
 上記方法で作製された単層フィルムを紙管に巻き取り、フィルム端面の着色度を肉眼で以下のように判定した。基準Cが実使用に耐えるボーダーレベルである。
 判定:基準
 A :着色なし
 B :わずかに黄変
 C :やや黄変
 D :黄変
(7) Appearance characteristics (whether or not yellowing occurs on the film end face)
The single-layer film produced by the above method was wound around a paper tube, and the degree of coloring of the film end face was determined with the naked eye as follows. Standard C is a border level that can withstand actual use.
Judgment: Criteria A: No coloring B: Slightly yellowing C: Slightly yellowing D: Yellowing
(8)繰り返し再利用時の着色性評価
 樹脂組成物ペレット2kgについて、東洋精機製作所社の20mm押出機「D2020」(D(mm)=20、L/D=20、圧縮比=2.0、スクリュー:フルフライト)を用いて以下の条件にてペレット化を行った。得られたEVOHペレットを再度同条件にてペレット化を行う操作を5回繰返し、最終的に得られたペレットの着色度の目視評価により、繰り返し再利用時の着色性を以下の判定基準により評価した。基準Cが実使用に耐えるボーダーレベルである。
〈ペレット化条件〉
  押出温度      供給部/圧縮部/計量部/ダイ
             =180/210/210/210℃
  スクリュー回転数  40rpm
  ダイ孔数      2穴
  凝固浴冷却水温度  30℃
〈繰り返し再利用後の着色度判定基準〉
 判定:基準
 A :ほとんど着色していない
 B :わずかに着色
 C :やや着色
 D :かなり着色
(8) Evaluation of colorability during repeated reuse About 2 kg of resin composition pellets, 20 mm extruder “D2020” (D (mm) = 20, L / D = 20, compression ratio = 2.0, Toyo Seiki Seisakusho Co., Ltd.) Using a screw: full flight, pelletization was performed under the following conditions. The operation of pelletizing the obtained EVOH pellets again under the same conditions is repeated 5 times, and the colorability at the time of repeated reuse is evaluated according to the following criteria by visual evaluation of the coloring degree of the finally obtained pellets. did. Standard C is a border level that can withstand actual use.
<Pelletization conditions>
Extrusion temperature Supply unit / Compression unit / Measuring unit / Die = 180/210/210/210 ° C.
Screw rotation speed 40rpm
Number of die holes 2 holes Solidification bath cooling water temperature 30 ° C
<Coloring criteria after repeated reuse>
Judgment: Criteria A: Almost not colored B: Slightly colored C: Slightly colored D: Very colored
(9)ロングラン性(ブツの経時的増加)
 樹脂組成物ペレット200gを用いて、熱風乾燥機にて210℃にて30分熱処理を行い、粉砕機にて粗粉砕(ペレットと同程度のサイズ)した。別途、熱処理を行っていないEVOHペレット2kgを準備し、前述の熱処理・粉砕後のEVOHを5質量%ブレンドしたものを用いて、東洋精機製作所社の20mm押出機「D2020」(D(mm)=20、L/D=20、圧縮比=2.0、スクリュー:フルフライト)を用いてペレット化を行った。押出条件は、供給部/圧縮部/計量部/ダイ=170/210/210/210℃とした。得られたペレットを用いて、東洋精機製作所社の20mm押出機「D2020」(D(mm)=20、L/D=20、圧縮比=2.0、スクリュー:フルフライト)を用いて上記(6)と同様の条件にて単層製膜を行った。製膜開始から30分後に得られた単層フィルムをサンプリングしてゲル状ブツ(肉眼で確認できる約150μm以上のもの)を数え、以下の判定基準により評価した。基準Cが実使用に耐えるボーダーレベルである。
 判定:基準
 A :ブツ個数10個以下/0.1m
 B :ブツ個数11個以上50個未満/0.1m
 C :ブツ個数50個以上300個未満/0.1m
 D :ブツ個数300個以上/0.1m
(9) Long-run (increased over time)
Using 200 g of the resin composition pellets, heat treatment was performed at 210 ° C. for 30 minutes with a hot air drier, and coarsely pulverized (same size as pellets) with a pulverizer. Separately, 2 kg of EVOH pellets that were not heat-treated were prepared, and a 20 mm extruder “D2020” (D (mm) = 20 and L / D = 20, compression ratio = 2.0, screw: full flight). The extrusion conditions were set to supply part / compression part / metering part / die = 170/210/210/210 ° C. Using the obtained pellets, a 20 mm extruder “D2020” (D (mm) = 20, L / D = 20, compression ratio = 2.0, screw: full flight) manufactured by Toyo Seiki Seisakusho Co., Ltd. A single-layer film was formed under the same conditions as in 6). A single layer film obtained 30 minutes after the start of film formation was sampled to count gel-like particles (about 150 μm or more that can be confirmed with the naked eye) and evaluated according to the following criteria. Standard C is a border level that can withstand actual use.
Judgment: Criteria A: Number of nuggets 10 or less / 0.1 m 2
B: The number of bumps is 11 or more and less than 50 / 0.1 m 2
C: 50 to less than 300 pieces / 0.1 m 2
D: 300 or more pieces / 0.1 m 2
(10)ロングラン性(スジ状外観不良の経時的増加)
 樹脂組成物ペレット5kgについて、東洋精機製作所社の20mm押出機「D2020」(D(mm)=20、L/D=20、圧縮比=2.0、スクリュー:フルフライト)を用いて単層製膜を行った。押出条件は、供給部/圧縮部/計量部/ダイ=190/210/210/210℃とした。スクリュー回転数100rpmにて20分間製膜運転を行った後、スクリューの回転を止め、押出機の温度設定を供給部/圧縮部/計量部/ダイ=150/150/150/150℃とした。スクリュー回転停止から3時間後、再び押出温度を、供給部/圧縮部/計量部/ダイ=190/210/210/210℃とし、スクリュー回転数100rpmにて単層製膜を行った。スクリュー回転を再開してから得られた単層フィルムをサンプリングしてゲル状ブツ(肉眼で確認できる約150μm以上のもの)を数え、ブツ数が10個以下/0.1mになるまでの時間を、スジ状外観不良の経時的増加に対応する指標として、以下の判定基準により評価した。基準Cが実使用に耐えるボーダーレベルである。
判定:基準
 A :ブツ個数が10個以下/0.1mになる時間が10分未満
 B :ブツ個数が10個以下/0.1mになる時間が10分以上30分未満
 C :ブツ個数が10個以下/0.1mになる時間が30分以上60分未満
 D :ブツ個数が10個以下/0.1mになる時間が60分以上
(10) Long run characteristics (Increase of streak-like appearance over time)
About 5 kg of resin composition pellets, manufactured by Toyo Seiki Seisakusho Co., Ltd. using a 20 mm extruder “D2020” (D (mm) = 20, L / D = 20, compression ratio = 2.0, screw: full flight) Membrane was performed. The extrusion conditions were set to supply part / compression part / metering part / die = 190/210/210/210 ° C. After performing the film forming operation at a screw rotation speed of 100 rpm for 20 minutes, the screw rotation was stopped and the temperature setting of the extruder was set to supply unit / compression unit / metering unit / die = 150/150/150/150 ° C. Three hours after the screw rotation stopped, the extrusion temperature was again set to supply part / compression part / metering part / die = 190/210/210/210 ° C., and a single-layer film was formed at a screw speed of 100 rpm. Sampling the single-layer film obtained after resuming screw rotation and counting gel-like spots (about 150 μm or more that can be confirmed with the naked eye) until the number of spots reaches 10 or less / 0.1 m 2 Was evaluated according to the following criteria as an index corresponding to the increase in the appearance of streaky appearance over time. Standard C is a border level that can withstand actual use.
Determination: reference A: seeding number is less than 10 or less /0.1m become time 2 is 10 minutes B: seeding number is less than 10 or 30 minutes or less /0.1m to become time 2 more than 10 minutes C: seeding number Is 10 minutes or less / 0.1 m 2 30 minutes or more and less than 60 minutes D: The time when the number of bumps is 10 pieces or less / 0.1 m 2 is 60 minutes or more
<実施例1>
 1-ヒドロキシエタン-1,1-ジホスホン酸(HEDP)が0.08g/L、酢酸ナトリウムが0.84g/L、酢酸が0.38g/L、ホウ酸が0.25g/Lとなるようにそれぞれの成分を水に溶解した水溶液92.4Lに、含水率105質量%の含水EVOHペレット(エチレン単位含有量(Et)32mol%、けん化度(DS)99.98mol%)を10.0kg投入して、25℃で6時間、時々攪拌しながら浸漬を行った。浸漬後のペレットを遠心脱水した後、熱風乾燥機中80℃で3時間、引き続き120℃で24時間乾燥して、樹脂組成物のペレットを得た。得られたペレットについて上記に従い分析した結果、1-ヒドロキシエタン-1,1-ジホスホン酸を30ppm、金属塩として酢酸ナトリウムを200ppm、モノカルボン酸として酢酸を200ppm、ホウ素化合物としてホウ酸を175ppm含んでいた。上記(7)外観特性(フィルム端面の黄変の発生の有無)の評価を行ったところ、フィルム端面には着色が見られずA判定であり、(8)繰り返し再利用時の着色性評価については着色がほとんどみられずA判定であった。また、(9)ロングラン性(ブツの経時的増加)についてはブツの数は10個以下/0.1mでA判定であった。
<Example 1>
1-hydroxyethane-1,1-diphosphonic acid (HEDP) is 0.08 g / L, sodium acetate is 0.84 g / L, acetic acid is 0.38 g / L, and boric acid is 0.25 g / L. 10.0 kg of hydrous EVOH pellets (ethylene unit content (Et) 32 mol%, saponification degree (DS) 99.98 mol%) having a water content of 105 mass% were added to 92.4 L of an aqueous solution in which each component was dissolved in water. Then, the immersion was performed at 25 ° C. for 6 hours with occasional stirring. The pellet after the immersion was subjected to centrifugal dehydration, and then dried in a hot air dryer at 80 ° C. for 3 hours and then at 120 ° C. for 24 hours to obtain a resin composition pellet. As a result of analyzing the obtained pellets according to the above, it contained 30 ppm of 1-hydroxyethane-1,1-diphosphonic acid, 200 ppm of sodium acetate as a metal salt, 200 ppm of acetic acid as a monocarboxylic acid, and 175 ppm of boric acid as a boron compound. It was. When the above-mentioned (7) appearance characteristics (whether or not yellowing of the film end face occurred) was evaluated, no color was seen on the film end face, and it was judged as A. (8) Colorability evaluation during repeated reuse No coloration was observed, and the determination was A. Further, (9) The long run property (increase in puncture over time) was judged as A with the number of lumps being 10 or less / 0.1 m 2 .
<実施例2~17及び比較例1~9>
 水溶液中に配合した成分及びその濃度を表1に示すように変更した以外は、実施例1と同様に操作することで、樹脂組成物のペレットを得た。得られた各ペレットについて、上記に従って分析及び評価した結果を表2に示す。なお、各表中のHEDPは、1-ヒドロキシエタン―1,1-ジホスホン酸であり、NTMPは、ニトロトリス(メチレンホスホン酸)であり、EDTMPは、エチレンジアミンテトラキス(メチレンホスホン酸)水和物である。
<Examples 2 to 17 and Comparative Examples 1 to 9>
Except having changed the component mix | blended in aqueous solution and its density | concentration as shown in Table 1, it operated similarly to Example 1 and obtained the pellet of the resin composition. Table 2 shows the results of analysis and evaluation of the obtained pellets according to the above. In each table, HEDP is 1-hydroxyethane-1,1-diphosphonic acid, NTMP is nitrotris (methylenephosphonic acid), and EDTMP is ethylenediaminetetrakis (methylenephosphonic acid) hydrate. .
<比較例19>
 ピロリン酸が0.89g/L、酢酸が1.4g/Lとなるようにそれぞれの成分を水に溶解した水溶液17.8Lに、含水率105質量%で酢酸ナトリウムを0.2%含有する含水EVOHペレット(エチレン単位含有量(Et)55mol%、けん化度(DS)97mol%)を10.0kg投入して、25℃で4時間、時々攪拌しながら浸漬を行った。浸漬後のペレットを遠心脱水した後、熱風乾燥機中80℃で3時間、引き続き120℃で24時間乾燥して、樹脂組成物のペレットを得た。得られたペレットについて、上記に従って分析及び評価した結果を表2に示す。
<Comparative Example 19>
Water content containing 0.2% sodium acetate at a water content of 105% by mass in 17.8 L of an aqueous solution in which the respective components are dissolved in water so that pyrophosphoric acid is 0.89 g / L and acetic acid is 1.4 g / L 10.0 kg of EVOH pellets (ethylene unit content (Et) 55 mol%, saponification degree (DS) 97 mol%) were added and immersed at 25 ° C. for 4 hours with occasional stirring. The pellet after the immersion was subjected to centrifugal dehydration, and then dried in a hot air dryer at 80 ° C. for 3 hours and then at 120 ° C. for 24 hours to obtain a resin composition pellet. Table 2 shows the results of analysis and evaluation of the obtained pellets according to the above.
<実施例18~20>
 用いた含水EVOHペレットの種類(EVOHのEt)並びに水溶液中に配合した成分及びその濃度を表1に示すように変更した以外は実施例1と同様に操作することで、樹脂組成物のペレットを得た。得られた各ペレットについて、上記に従って分析及び評価した結果を表2に示す。
<Examples 18 to 20>
By operating in the same manner as in Example 1 except that the types of hydrous EVOH pellets used (Et of EVOH), the components blended in the aqueous solution, and the concentrations thereof were changed as shown in Table 1, pellets of the resin composition were obtained. Obtained. Table 2 shows the results of analysis and evaluation of the obtained pellets according to the above.
Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000002
Figure JPOXMLDOC01-appb-T000002
 表2に示すように、樹脂組成物が、特定のリン化合物と金属塩とを特定の量で含有する場合、全ての評価項目でC以上の判定となり、耐着色性、及びブツの経時的増加が抑制されるといったロングラン性に優れる樹脂組成物を得ることができた。また、モノカルボン酸及びホウ酸を所定の量で含有させることで、上記特性をさらに向上することができた。 As shown in Table 2, when the resin composition contains a specific phosphorus compound and a metal salt in a specific amount, it becomes a determination of C or more in all evaluation items, and the color resistance and the time-dependent increase in the thickness It was possible to obtain a resin composition having excellent long-run properties such as suppression of corrosion. Moreover, the said characteristic was further improved by containing monocarboxylic acid and boric acid in a predetermined quantity.
<実施例21>
 水溶液中に配合した成分及びその濃度を表3に示すように変更した以外は、実施例1と同様に操作することで、樹脂組成物のペレットを得た。得られたペレットについて上記に従って分析した結果を表4に示す。上記(7)外観特性(フィルム端面の黄変の発生の有無)の評価を行ったところ、フィルム端面には着色が見られずA判定であり、(8)繰り返し再利用時の着色性評価については着色がほとんどみられずA判定であった。また、(10)ロングラン性(スジ状外観不良の経時的増加)についてはブツ個数が10個以下/0.1mになる時間が10分未満であり、A判定であった。
<Example 21>
Except having changed the component mix | blended in aqueous solution and its density | concentration as shown in Table 3, it operated similarly to Example 1 and the pellet of the resin composition was obtained. Table 4 shows the results of analyzing the obtained pellets according to the above. When the above-mentioned (7) appearance characteristics (whether or not yellowing of the film end face occurred) was evaluated, no color was seen on the film end face, and it was judged as A. (8) Colorability evaluation during repeated reuse No coloration was observed, and the determination was A. In addition, (10) Long run property (time-dependent increase in streak-like appearance defect) was less than 10 minutes for the number of bumps to be 10 or less / 0.1 m 2 , and was judged as A.
<実施例22~31及び比較例10~18>
 水溶液中に配合した成分及びその濃度を表3に示すように変更した以外は、実施例21と同様に操作することで、樹脂組成物のペレットを得た。得られた各ペレットについて、上記に従って分析及び評価した結果を表4に示す。
<Examples 22 to 31 and Comparative Examples 10 to 18>
Except having changed the component mix | blended in aqueous solution and its density | concentration as shown in Table 3, it operated similarly to Example 21, and the pellet of the resin composition was obtained. Table 4 shows the results of analysis and evaluation of the obtained pellets according to the above.
<実施例32~34>
 用いた含水EVOHペレットの種類(EVOHのEt)並びに水溶液中に配合した成分及びその濃度を表3に示すように変更した以外は実施例21と同様に操作することで、樹脂組成物のペレットを得た。得られた各ペレットについて、上記に従って分析及び評価した結果を表4に示す。
<Examples 32 to 34>
The pellets of the resin composition were prepared by operating in the same manner as in Example 21 except that the types of hydrous EVOH pellets used (Et of EVOH) and the components and concentrations thereof contained in the aqueous solution were changed as shown in Table 3. Obtained. Table 4 shows the results of analysis and evaluation of the obtained pellets according to the above.
Figure JPOXMLDOC01-appb-T000003
Figure JPOXMLDOC01-appb-T000003
Figure JPOXMLDOC01-appb-T000004
Figure JPOXMLDOC01-appb-T000004
 表4に示すように、樹脂組成物が、特定のリン化合物と金属塩とを所定の量で含有する場合、全ての評価項目でC以上の判定となり、耐着色性、及び長時間の成形においてもフィッシュアイやスジ等が生じないといったロングラン性に優れる樹脂組成物を得ることができた。また、モノカルボン酸及びホウ酸を所定の量で含有させることで、上記特性をさらに向上することができた。 As shown in Table 4, when the resin composition contains a specific phosphorus compound and a metal salt in a predetermined amount, it becomes a determination of C or more in all evaluation items, and in coloration resistance and long-time molding In addition, it was possible to obtain a resin composition excellent in long run properties such that fish eyes and streaks are not generated. Moreover, the said characteristic was further improved by containing monocarboxylic acid and boric acid in a predetermined quantity.

Claims (7)

  1.  エチレン-ビニルアルコール共重合体を主成分とする樹脂組成物であって、
     リン化合物及び金属塩を含有し、
     上記リン化合物が、縮合リン酸、2つ以上のホスホン酸基を有する化合物又はこれらの組み合わせであり、
     上記リン化合物の含有量が0.1ppm以上50ppm未満であり、
     上記金属塩の含有量が金属元素換算で5ppm以上500ppm以下であることを特徴とする樹脂組成物。
    A resin composition comprising an ethylene-vinyl alcohol copolymer as a main component,
    Containing a phosphorus compound and a metal salt;
    The phosphorus compound is condensed phosphoric acid, a compound having two or more phosphonic acid groups, or a combination thereof;
    The phosphorus compound content is 0.1 ppm or more and less than 50 ppm,
    Content of the said metal salt is 5 ppm or more and 500 ppm or less in conversion of a metal element, The resin composition characterized by the above-mentioned.
  2.  上記金属塩がアルカリ金属塩、アルカリ土類金属塩又はこれらの組み合わせである請求項1に記載の樹脂組成物。 The resin composition according to claim 1, wherein the metal salt is an alkali metal salt, an alkaline earth metal salt, or a combination thereof.
  3.  上記金属塩がアルカリ金属塩である請求項2に記載の樹脂組成物。 The resin composition according to claim 2, wherein the metal salt is an alkali metal salt.
  4.  上記金属塩がアルカリ土類金属塩であり、
     上記アルカリ土類金属塩の含有量が金属元素換算で5ppm以上100ppm以下である請求項2に記載の樹脂組成物。
    The metal salt is an alkaline earth metal salt;
    The resin composition according to claim 2, wherein the content of the alkaline earth metal salt is 5 ppm or more and 100 ppm or less in terms of a metal element.
  5.  モノカルボン酸をさらに含有し、
     上記モノカルボン酸の含有量が5ppm以上500ppm以下である請求項1から請求項4のいずれか1項に記載の樹脂組成物。
    Further containing a monocarboxylic acid,
    The resin composition according to any one of claims 1 to 4, wherein a content of the monocarboxylic acid is 5 ppm or more and 500 ppm or less.
  6.  ホウ素化合物をさらに含有し、
     上記ホウ素化合物の含有量がホウ素元素換算で5ppm以上2,000ppm以下である請求項1から請求項5のいずれか1項に記載の樹脂組成物。
    Further containing a boron compound,
    The resin composition according to any one of claims 1 to 5, wherein a content of the boron compound is 5 ppm or more and 2,000 ppm or less in terms of boron element.
  7.  請求項1から請求項6のいずれか1項に記載の樹脂組成物から形成される部分を有する成形体。 A molded body having a portion formed from the resin composition according to any one of claims 1 to 6.
PCT/JP2016/086951 2015-12-25 2016-12-12 Resin composition and molded article WO2017110568A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN201680075588.4A CN108473744B (en) 2015-12-25 2016-12-12 Resin composition and molded article
JP2017557889A JP6704415B2 (en) 2015-12-25 2016-12-12 Resin composition and molded article

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2015-254817 2015-12-25
JP2015254817 2015-12-25

Publications (1)

Publication Number Publication Date
WO2017110568A1 true WO2017110568A1 (en) 2017-06-29

Family

ID=59090176

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2016/086951 WO2017110568A1 (en) 2015-12-25 2016-12-12 Resin composition and molded article

Country Status (4)

Country Link
JP (1) JP6704415B2 (en)
CN (1) CN108473744B (en)
TW (1) TWI622614B (en)
WO (1) WO2017110568A1 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2020084017A (en) * 2018-11-22 2020-06-04 株式会社クラレ Blow molded container, and fuel container and bottle container each comprising the same
JP2020083374A (en) * 2018-11-22 2020-06-04 株式会社クラレ Thermoforming container
JP2020082495A (en) * 2018-11-22 2020-06-04 株式会社クラレ Vapor-deposited film, packaging material, and vacuum insulation body
JP2020090646A (en) * 2017-12-28 2020-06-11 株式会社クラレ Resin composition, manufacturing method therefor, molded body, and multilayer structure
US20210115237A1 (en) * 2018-03-29 2021-04-22 Dow Global Technologies Llc Bicomponent fiber and polymer composition thereof
DE112020005638T5 (en) 2019-12-27 2022-08-25 Kuraray Co., Ltd. RESIN COMPOSITION, AND MOLDED OBJECT AND MULTILAYER STRUCTURE EACH COMPRISING THESE
US11739187B2 (en) 2017-12-28 2023-08-29 Kuraray Co., Ltd. Resin composition, production method thereof, molded product, multilayer structure, film, production method thereof, vapor deposition film, packaging material, vacuum packaging bag, vacuum insulator, thermoformed container, blow molded container, fuel container, and bottle-shaped container

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5022050A (en) * 1973-06-26 1975-03-08
JPH0297543A (en) * 1988-07-19 1990-04-10 Nippon Synthetic Chem Ind Co Ltd:The Resin composition
JP2001049053A (en) * 1999-08-06 2001-02-20 Dainippon Ink & Chem Inc Resin composition and its molded product
JP2001146539A (en) * 1999-09-07 2001-05-29 Kuraray Co Ltd Resin composition comprising ethylene/vinyl alcohol copolymer having low odor and excellent interlaminar bonding and multilayered structure using the same
JP2001164059A (en) * 1999-09-29 2001-06-19 Kuraray Co Ltd Resin composition comprising ethylene-vinyl alcohol copolymer having excellent long run property and multilayer structure using the composition
JP2001261855A (en) * 2000-03-14 2001-09-26 Sumitomo Bakelite Co Ltd Fire retardant sheet
JP2001294674A (en) * 2000-04-17 2001-10-23 Unitica Fibers Ltd Soft reinforced fiber sheet
JP2001347612A (en) * 2000-06-06 2001-12-18 Kuraray Co Ltd Multilayer structure
JP2003246907A (en) * 2002-02-27 2003-09-05 Nippon Synthetic Chem Ind Co Ltd:The Polyvinyl alcohol film
JP2009191255A (en) * 2008-01-15 2009-08-27 Nippon Synthetic Chem Ind Co Ltd:The Resin composition and laminate
WO2011078198A1 (en) * 2009-12-21 2011-06-30 住友化学株式会社 Resin composition
CN103012971A (en) * 2012-12-04 2013-04-03 合肥杰事杰新材料股份有限公司 EPDM/EVOH-MAA (ethylene-propylene-diene monomer/ethylene vinyl alcohol-methacrylic acid) dynamically vulcanizled thermoplastic elastomer for separating gas and resisting water vapor and preparation method thereof
WO2015053176A1 (en) * 2013-10-09 2015-04-16 日本合成化学工業株式会社 Saponified ethylene-vinyl ester copolymer composition, and multilayer structure using said composition

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5032632A (en) * 1990-05-15 1991-07-16 E. I. Du Pont De Nemours And Company Oxidation-resistant ethylene vinyl alcohol polymer compositions
DE69715778T2 (en) * 1996-11-19 2003-08-14 Kuraray Co Resin composition and multilayer structure
ES2386666T3 (en) * 1998-10-07 2012-08-24 Kuraray Co., Ltd. Multilayer structure and process to produce it
SG184248A1 (en) * 2010-03-25 2012-11-29 Kuraray Co Resin composition, method for production thereof and multilayered structure

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5022050A (en) * 1973-06-26 1975-03-08
JPH0297543A (en) * 1988-07-19 1990-04-10 Nippon Synthetic Chem Ind Co Ltd:The Resin composition
JP2001049053A (en) * 1999-08-06 2001-02-20 Dainippon Ink & Chem Inc Resin composition and its molded product
JP2001146539A (en) * 1999-09-07 2001-05-29 Kuraray Co Ltd Resin composition comprising ethylene/vinyl alcohol copolymer having low odor and excellent interlaminar bonding and multilayered structure using the same
JP2001164059A (en) * 1999-09-29 2001-06-19 Kuraray Co Ltd Resin composition comprising ethylene-vinyl alcohol copolymer having excellent long run property and multilayer structure using the composition
JP2001261855A (en) * 2000-03-14 2001-09-26 Sumitomo Bakelite Co Ltd Fire retardant sheet
JP2001294674A (en) * 2000-04-17 2001-10-23 Unitica Fibers Ltd Soft reinforced fiber sheet
JP2001347612A (en) * 2000-06-06 2001-12-18 Kuraray Co Ltd Multilayer structure
JP2003246907A (en) * 2002-02-27 2003-09-05 Nippon Synthetic Chem Ind Co Ltd:The Polyvinyl alcohol film
JP2009191255A (en) * 2008-01-15 2009-08-27 Nippon Synthetic Chem Ind Co Ltd:The Resin composition and laminate
WO2011078198A1 (en) * 2009-12-21 2011-06-30 住友化学株式会社 Resin composition
CN103012971A (en) * 2012-12-04 2013-04-03 合肥杰事杰新材料股份有限公司 EPDM/EVOH-MAA (ethylene-propylene-diene monomer/ethylene vinyl alcohol-methacrylic acid) dynamically vulcanizled thermoplastic elastomer for separating gas and resisting water vapor and preparation method thereof
WO2015053176A1 (en) * 2013-10-09 2015-04-16 日本合成化学工業株式会社 Saponified ethylene-vinyl ester copolymer composition, and multilayer structure using said composition

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2020090646A (en) * 2017-12-28 2020-06-11 株式会社クラレ Resin composition, manufacturing method therefor, molded body, and multilayer structure
JP7237570B2 (en) 2017-12-28 2023-03-13 株式会社クラレ Resin composition, method for producing the same, molded article, and multilayer structure
US11739187B2 (en) 2017-12-28 2023-08-29 Kuraray Co., Ltd. Resin composition, production method thereof, molded product, multilayer structure, film, production method thereof, vapor deposition film, packaging material, vacuum packaging bag, vacuum insulator, thermoformed container, blow molded container, fuel container, and bottle-shaped container
US20210115237A1 (en) * 2018-03-29 2021-04-22 Dow Global Technologies Llc Bicomponent fiber and polymer composition thereof
JP2020084017A (en) * 2018-11-22 2020-06-04 株式会社クラレ Blow molded container, and fuel container and bottle container each comprising the same
JP2020083374A (en) * 2018-11-22 2020-06-04 株式会社クラレ Thermoforming container
JP2020082495A (en) * 2018-11-22 2020-06-04 株式会社クラレ Vapor-deposited film, packaging material, and vacuum insulation body
JP7195891B2 (en) 2018-11-22 2022-12-26 株式会社クラレ Metallized films, packaging materials, and vacuum insulators
JP7199932B2 (en) 2018-11-22 2023-01-06 株式会社クラレ thermoformed container
JP7246169B2 (en) 2018-11-22 2023-03-27 株式会社クラレ Blow-molded container, and fuel container and bottle container comprising the same
DE112020005638T5 (en) 2019-12-27 2022-08-25 Kuraray Co., Ltd. RESIN COMPOSITION, AND MOLDED OBJECT AND MULTILAYER STRUCTURE EACH COMPRISING THESE

Also Published As

Publication number Publication date
JPWO2017110568A1 (en) 2018-10-11
TWI622614B (en) 2018-05-01
TW201734110A (en) 2017-10-01
CN108473744A (en) 2018-08-31
CN108473744B (en) 2020-08-04
JP6704415B2 (en) 2020-06-03

Similar Documents

Publication Publication Date Title
JP6704415B2 (en) Resin composition and molded article
KR101795094B1 (en) Resin composition, process for production thereof, and multilayer structure
US7323503B2 (en) Process for producing ethylene-vinyl alcohol copolymer resin, process for producing pellets and resin pellets
JP3590498B2 (en) Saponified ethylene-vinyl ester copolymer composition and co-extruded multilayer molded article using the same
JP5944388B2 (en) Ethylene-vinyl alcohol copolymer resin composition and method for producing the same
JP6724019B2 (en) Resin composition, method for producing the same, and multilayer structure
JP4954514B2 (en) Ethylene-vinyl alcohol copolymer resin composition
JP2001164059A (en) Resin composition comprising ethylene-vinyl alcohol copolymer having excellent long run property and multilayer structure using the composition
JP2020090646A (en) Resin composition, manufacturing method therefor, molded body, and multilayer structure
JP7337593B2 (en) Pellets, melt-molded products made from the same, and methods for producing the same
JP3704448B2 (en) Process for producing ethylene-vinyl alcohol copolymer resin pellets and resin pellets
JP4480826B2 (en) Method for producing ethylene-vinyl alcohol copolymer resin pellets
JP4046245B2 (en) Process for producing saponified ethylene-vinyl acetate copolymer
JP2001146539A (en) Resin composition comprising ethylene/vinyl alcohol copolymer having low odor and excellent interlaminar bonding and multilayered structure using the same
JP2001164070A (en) Resin composition composed of ethylene-vinyl alcohol copolymer having low odor
JP6733059B1 (en) Ethylene-vinyl alcohol copolymer and method for producing the same
JP2006282833A (en) Ethylene-vinyl alcohol copolymer, ethylene-vinyl alcohol copolymer resin composition, and method for producing the same
JP4588146B2 (en) Method for producing ethylene-vinyl alcohol copolymer resin and method for producing pellets
JPWO2019130989A1 (en) Ethylene-vinyl alcohol copolymer-containing resin composition, and molded articles and packaging materials comprising the same.
JP2001072823A (en) Resin composition comprising ethylene-vinyl alcohol copolymer and multilayer structure using the same
JP5093959B2 (en) Ethylene-vinyl alcohol copolymer resin composition
JP2001098080A (en) Method for production of ethylene/vinyl alcohol copolymer resin composition
JP2005329718A (en) Manufacturing method of ethylene-vinyl alcohol copolymer resin pellets and resin pellets
JPWO2019130799A1 (en) Ethylene-vinyl alcohol copolymer-containing resin composition, molded product and packaging material
JP3976809B2 (en) Process for treating saponified ethylene-vinyl ester copolymer

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 16878459

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 2017557889

Country of ref document: JP

Kind code of ref document: A

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 16878459

Country of ref document: EP

Kind code of ref document: A1