Resin composition and multilayered structure

Abstract: A resin composition is disclosed, comprising a copolymer (A) comprising ethylene as a major component produced by using a single-site catalyst, and an ethylene-vinyl alcohol copolymer (B) having an ethylene content of 20 to 60 mol% and a degree of hydrolysis of 95% or above, said resin composition satisfying the following equation (1): 1/99 ≤ {weight of (A)}/{weight of (B)} ≤ 99/1 A preferred resin composition is one in which the copolymer (A) has a density of 0.90 to 0.94 g/cm 3 and the resin composition further comprises a carboxylic acid-modified polyolefin (C) and satisfies the following equations (2) and (3): 60/40 ≤ {weight of (A)}/{weight of (B)} ≤ 99/1 0.1/99.9 ≤ X ≤ 20/80 wherein X = {weight of (C)}/{total weight of (A) and (B)} . Another preferred resin composition is one in which the copolymer (A) has a density of 0.85 to 0.90 g/cm 3 , and the resin composition satisfies the following equation (5): 1/99 ≤ {weight of (A)}/{weight of (B)} ≤ 40/60 The resin composition is superior in melt moldability, gas barrier properties, flexural fatigue resistance, and impact resistance. It can be used for a layer of multilayered structure to impart a good appearance, delamination resistance, transparency, impact resistance, and gas barrier properties.

Description: The present invention relates to a resin composition superior in melt molding properties, gas barrier properties, flexural fatigue resistance, and impact resistance. The present invention also relates to a multilayered structure, particularly one which has good appearance, good delamination resistance, good transparency, good impact resistance, and good gas barrier properties. An ethylene-vinyl alcohol copolymer (occasionally referred to as EVOH hereinafter) finds general use because of its good melt molding properties and gas barrier properties. In particular, it is used in the form of multilayered plastic packaging material after lamination with a thermoplastic resin (especially polyolefin resin) superior in moisture resistance and mechanical properties. This packaging material finds applications as e.g. bags, bottles, cups or pouches in a variety of areas (including foods, cosmetics, medicines, chemicals, and toiletries) on account of its good oxygen barrier properties. Production of multilayered plastic containers inevitably gives rise to regrinds (scraps), such as edges trimmed from extruded sheets and films, flashes pinched off from blow-molded bottles, and scraps punched off from molded cups. Recycling of these regrinds is necessary for cost and material saving. To this end, there have been proposed a method for utilizing regrinds by incorporating them into layers of thermoplastic resin (such as polyolefin) as a major constituent (JP-B-59-29409) and a method for utilizing regrinds by interposing a layer of regrinds between a layer of thermoplastic (such as polyolefin) and a layer of EVOH (JP-A-59-101338). The recycling of regrinds in the above-mentioned manner presents several difficulties. That is, when a thermoplastic resin (especially polyolefin resin) and EVOH are extruded together with regrinds, EVOH tends to deteriorate, giving rise to black scorches stuck inside the extruder and gel-like substance (gum) attached to the die lip of the extruder. Moreover, deterioration of EVOH is accompanied by heterogeneous phase separation (to give foreign matter) and anomalous flow. This results in containers having a poor appearance, having an odor of decomposed resin, and having poor mechanical properties (such as impact resistance). These difficulties prevent the normal extrusion operation or restrict the operation time. In addition, the presence of regrinds causes a wavy pattern to the surface of the molded article or causes interlayer or intralayer delamination when a blend composition of polyolefin and EVOH is coextruded with EVOH or polyolefin. One way to address this problem is to incorporate the blend of EVOH and polyolefin resin with a polar group-modified polyolefin (typified by carboxylic acid-modified polyolefin), as disclosed in JP-A-49-57086, 3-72539, 5-98084, 61-111346, and 8-27332. On the other hand, EVOH has the disadvantage of being poor in flexibility, flexural fatigue resistance, and impact resistance. Therefore, it is not necessarily suitable for flexible bags and pouches, which need good flexural fatigue resistance, and bottles and cups, which need good impact resistance. One way to improve EVOH in impact resistance and flexural resistance is to incorporate a soft polyolefin into EVOH. An example of the soft polyolefin is a low-density polyethylene having density of 0.086 to 0.91 g/cm 3 , produced by using a Ziegler catalyst; see JP-A-62-153333. Nevertheless, the object of improving impact resistance and flexural resistance has not been achieved satisfactorily. A new polyolefin is attracting attention which is produced by using a single-site catalyst having uniform polymerization active sites. As compared with conventional polyolefins, it has a narrower molecular weight distribution and composition distribution. Consequently, it is superior in transparency, strength, adhesiveness, heat-sealability, impact resistance, leaching resistance, and blocking resistance. It is under extensive study for development. The ethylene-α-olefin copolymer produced by using a single-site catalyst finds many uses in the form of laminate with EVOH. Applications of the laminate include packaging laminate film (JP-A-7-232418), coextrusion film (JP-A-7-314624), multilayered film for balloon forming (JP-A-7-284570), heat-shrinkable film (JP-A-7-309962), and retort packaging material (JP-A-7-266520). These patent publications, however, do not mention anything about compositions of EVOH and ethylene-α-olefin copolymer and the recycling of regrinds. There is disclosed a laminate in JP-A-7-102133 which is made up of a layer of EVOH and a layer of a resin composition comprising an ethylene-α-olefin copolymer produced by using a single-site catalyst and a carboxylic acid-modified polyolefin. This resin composition is designed so as to provide good adhesiveness for a variety of resins such as nylon, EVOH, polyester, and ethylene-vinyl acetate copolymer. Therefore, this patent application does not mention anything about the composition comprising an ethylene-α-olefin copolymer, a carboxylic acid-modified polyolefin, and EVOH, nor does it mention about the laminate having a layer of regrinds. There is disclosed a laminate in JP-A-7-329262 which is made up of a layer of a composition comprising recovered polyethylene produced by using a conventional catalyst and carboxylic acid-modified polyolefin, a layer of ethylene-α-olefin copolymer produced by using a single-site catalyst, and a layer of EVOH. The laminate is characterized by good adhesion between the first two layers. This patent application, however, does not mention anything about incorporating the ethylene-α-olefin copolymer produced by using a single-site catalyst with EVOH and further with a carboxylic acid-modified polyolefin. There is disclosed a laminate in JP-A-6-166157 which is made up of a layer of syndiotactic polypropylene produced by using a single-site catalyst, a layer of EVOH, a layer of a carboxylic acid-modified polyolefin, and a layer of regrinds. This patent publication, however, does not mention anything about the composition used for the layer of regrinds. In addition, the laminate does not have a layer of an ethylene-α-olefin copolymer produced by using a single-site catalyst. An ethylene-α-olefin copolymer produced by using a single-site catalyst displays marked characteristics when used as a laminate with EVOH, as mentioned above. Production of laminates accompanies regrinds, and an effective use of regrinds is an important economical subject for material saving. Unfortunately, there is no known way of utilizing regrinds containing said copolymer and EVOH. In addition, nothing is known about the difference between regrinds containing said copolymer and regrinds containing a conventional copolymer (produced by using Ziegler catalyst). The present invention offers a new resin composition suitable for said regrinds which is characterized by its specific resin, compatibilizing agent, compounding ratio, and dispersing mode. The resin composition has improved melt moldability and permits its regrinds to be recycled effectively. The present invention also offers a multilayered structure (or molded article) superior in appearance, delamination resistance, transparency, impact resistance, and gas barrier properties. According to the present invention, a new resin composition is also obtained by incorporating EVOH with a copolymer comprising ethylene as a major component in a specific ratio. The resulting EVOH-based resin composition has improved impact resistance, flexural fatigue resistance, and gas barrier properties. It is an object of the present invention to provide a resin composition which comprises a copolymer (A) comprising ethylene as a major component (sometimes referred to simply as "copolymer (A)" or "ethylene copolymer (A)" hereinafter) produced by using a single-site catalyst, and an ethylene-vinyl alcohol copolymer (B) having an ethylene content of 20 to 60 mol% and a degree of hydrolysis of 95% or above, said resin composition satisfying the following equation (1): 1/99 ≤ {weight of (A)}/{weight of (B)} ≤ 99/1 The copolymer (A) is preferably an ethylene-α-olefin copolymer in which the α-olefin has 3 to 8 carbon atoms and/or which has a molecular weight distribution (Mw/Mn) of not greater than 4. In one embodiment, the ethylene-vinyl alcohol copolymer (B) is preferably one which contains a phosphorus compound in an amount of 2 to 200 ppm in terms of phosphorus element. The resin composition is preferably one in which the copolymer (A) has a density of 0.90 to 0.94 g/cm 3 and which further comprises a carboxylic acid-modified polyolefin (C) and satisfies the following equations (2) and (3): 60/40 ≤ {weight of (A)}/{weight of (B)} ≤ 99/1 0.1/99.9 ≤ X ≤ 20/80 wherein X = {weight of (C)}/{total weight of (A) and (B)}. The resin composition is preferably one in which the resin particles of the ethylene-vinyl alcohol copolymer (B) and the carboxylic acid-modified polyethylene (C) are dispersed in a matrix of the copolymer (A), and have an average particle diameter not greater than 5 µm. The resin composition is preferably one in which the melt flow rate Ma of the copolymer (A) and the melt flow rate Mb of the ethylene-vinyl alcohol copolymer (B) satisfy the following equation (4): 0.05 ≤ Ma/Mb ≤ 5 The resin composition is preferably one which further comprises a hydrotalcite compound (D) in an amount of 0.0001 to 2% based on the total weight of (A) and (B) and/or a metal salt of a higher aliphatic carboxylic acid (E) in an amount of 0.0001 to 2% based on the total weight of (A) and (B). It is another object of the present invention to provide a multilayered structure which comprises a layer of the resin composition defined above and a layer of an ethylene-vinyl alcohol copolymer having an ethylene content of 20 to 60 mol% and a degree of hydrolysis of 95% or above. The multilayered structure is preferably one which further comprises at least one layer comprising an ethylene-α-olefin copolymer produced by using a single-site catalyst and having a density of 0.90 to 0.94 g/cm 3 , in which the α-olefin has 3 to 8 carbon atoms and a carboxylic acid-modified polyolefin. The multilayered structure is preferably one which is formed by coextrusion. In another embodiment, the resin composition is preferably one in which the copolymer (A) has a density of 0.85 to 0.90 g/cm 3 and which satisfies the following equation (5) : 1/99 ≤ {weight of (A)}/{weight of (B)} ≤ 40/60 The resin composition is preferably one in which the melt flow rate Ma of the copolymer (A) and the melt flow rate Mb of the ethylene-vinyl alcohol copolymer (B) satisfy the following equation (6): 0.2 ≤ Ma/Mb ≤ 20 The resin composition is preferably one which further comprises a carboxylic acid-modified polyolefin (C) and satisfies the following equation (7): 0.1/99.9 ≤ X ≤ 20/80 where X = {weight of (C)}/{total weight of (A) and (B)} In a preferred embodiment, the multilayered structure comprises a layer of the resin composition defined above, a layer of adhesive resin, and a layer of polyolefin. It is another object of the present invention to provide a bag-in-box container comprising the multilayered structure defined above, wherein a core layer of the resin composition is laminated with inner and outer layers of an ethylene-α-olefin copolymer via layers of adhesive resin. In the present invention, the copolymer (A) is one produced by using a single-site catalyst. The copolymer comprising ethylene as a major component as referred to throughout the specification and appended claims is one having an ethylene content of 50 wt% or more. The comonomer to be copolymerized with ethylene is not particularly restricted. Examples of the comonomer which can be used are exemplified below. An α-olefin selected from propylene, 1-butene, 1-hexene, 1-octene, and 4-methyl-1-pentene. A vinyl compound selected from styrene, diolefins, N-vinylcarbazole, vinyl chloride, vinylidene chloride, vinyl acetate, acrylonitrile, and vinyl ether. An unsaturated carboxylic acid selected from maleic acid, acrylic acid, methacrylic acid, ethacrylic acid, fumaric acid, and itaconic acid, or esters or anhydrides thereof, with or without a hydroxyl group or epoxy group added thereto. Preferred examples of the comonomer to be copolymerized with ethylene include C 3-8 α-olefins, such as propylene, 1-butene, isobutene, 1-pentene, 1-hexene, 1-heptene, 1-octene, 3-methyl-1-butene, 4-methyl-1-pentene, and 4,4-dimethyl-1-pentene. They may be use alone or in combination with one another. Of these examples, 1-butene, isobutene, 1-pentene, 1-hexene, 1-octene, and 4-methyl-1-pentene are desirable because of their low price and their flexibility in controlling the copolymer make-up. Comonomers having 9 or more carbon atoms are not desirable because of their high price and low reactivity (leading to difficulties in their introduction into the copolymer). In the present invention, the single-site catalyst means a catalyst characterized by uniform active sites. Its typical examples include metallocene catalysts. In actual use for olefin polymerization, a metallocene compound is preferably used in combination with an organoaluminum compound (typified by aluminoxane) or a compound with which it reacts to form a stable anion. The metallocene transition metal compound used in the present invention is a compound in which at least one ligand having the cyclopentadienyl skeleton is attached (η 5 ) to the metal belonging to Groups 3 to 10 or lanthanum series of the periodic table. Examples of the metal include titanium, zirconium, hafnium, vanadium, niobium, tantalum, chromium, lanthanum, nickel, palladium, rhodium, and iridium. Preferable among these examples are titanium, zirconium, hafnium, vanadium, nickel, and palladium. Examples of the ligand having cyclopentadienyl groups or substituted cyclopentadienyl groups include cyclopentadienyl group, alkyl-substituted cyclopentadienyl group, indenyl group, alkyl-substituted indenyl group, 1,5,6,7-tetrahydroindenyl group, alkyl-substituted 1,5,6,7-tetrahydroindenyl group, fluorenyl group, and alkyl-substituted fluorenyl group. In these groups the substituent alkyl group may be substituted with halogen atoms or trialkylsilyl groups. Of these ligands, the cyclopentadienyl group and alkyl-substitute cyclopentadieny group are particularly desirable. In case where one molecule of the metallocene compound contains two or more cyclopentadienyl groups, those groups having them may be bonded to each other through an alkylene group (such as ethylene, propylene, and isopropylidene) or a substituted silylene group (such as diphenylsilylene and methylphenylsilylene). Examples of the metallocene compounds include cyclopentadienyltitaniumtris(dimethylamide), methylcyclopentadiethyltitaniumtris(dimethylamide), bis(cyclopentadienyl)titanium dichloride, dimethylsilyltetramethylcyclopentadienyl-t-butylamidezirconium dichloride, dimethylsilyltetramethylcyclopentadienyl-t-butylamidehafnium dichloride, dimethylsilyltetramethylcyclopentadienyl-p-n-butylphenylamidezirconium dichloride, methylphenylsilyltetramethylcyclopentatdienyl-t-butylamidehafnium dichloride, (t-butylamide)(tetramethylcyclopentadienyl)-1,2-ethanediyltitanium dichloride, indenyltitaniumtris(dimethylamide), indenyltitaniumtris(diethylamide), indenyltitaniumbis(di-n-butylamide), and indenyltitaniumbis(di-n-propylamide). Another single-site catalyst is a metal-diimine complex compound, whose examples are listed below. N,N'-bis(diisopropylphenyl)diimine nickel dibromide, N,N'-bis(diisopropylphenyl)diimine nickel dichloride, N,N'-bis(diisopropylphenyl)diimine nickel dimethyl, N,N'-bis(diisopropylphenyl)diimine palladium dibromide, N,N'-bis(diisopropylphenyl)diimine palladium dichloride, N,N'-bis(diisopropylphenyl)diimine palladium dimethyl, N,N'-bis(dimethylphenyl)diimine nickel dibromide, N,N'-bis(dimethylphenyl)diimine nickel dichloride, N,N'-bis(dimethylphenyl)diimine nickel dimethyl, N,N'-bis(dimethylphenyl)diimine palladium dibromide, N,N'-bisN,N'-bis(dimethylphenyl)diimine palladium dichloride, and N,N'-bisN,N'-bis(dimethylphenyl)diimine palladium dimethyl. These single-site catalysts are used in combination with an activating cocatalyst, which is an aluminum compound having an Al-O bond, such as a linear or cyclic aluminoxane. The aluminoxane is formed when alkylaluminum comes into contact with water. In other words, it is obtained when alkylaluminum is added to the system at the time of polymerization and water is added to the system afterwards, or if alkylaluminum is reacted with water of crystallization in the complex or absorbed water in inorganic compounds. Examples of the alkylaluminum include triethylaluminum, triisobutylaluminum, dimethylaluminum chloride, diethylaluminum chloride, methylaluminum dichloride, ethylaluminum dichloride, dimethylaluminum fluoride, diisobutylaluminum hydride, diethylaluminum hydride, and ethylaluminum sesquichloride. Examples of the component which reacts with the metallocene compound to form a stable anion include an organoboron compound anion, organoaluminum compound anion, organogallium compound anion, organophosphorus compound anion, organosilicon compound anion, organoarsenic compound anion, and organoantimony compound anion. There are no specific restrictions on the conditions of polymerization by the single-site catalyst. It is possible to carry out polymerization batchwise or continuously in the same manner as in polymerization by a Ziegler catalyst, such as bulk polymerization, solution polymerization, suspension polymerization, and gas-phase polymerization. Highpressure ion polymerization at 1 to 100 atms., preferably 1 to 50 atms., and at 0 to 250°C, preferably 25 to 200°C, is preferable. The copolymer (A) produced by using a single-site catalyst has a melt flow rate (MFR) of 0.1 to 50 g/min, preferably 0.5 to 30 g/min (measured at 210°C under a load of 2,160 g), although it is not specifically restricted in MFR. The object of the present invention is achieved by using the copolymer comprising ethylene as a major component produced by using a single-site catalyst. If this copolymer is replaced by the conventional one (produced by using a Ziegler catalyst), the resulting composition is not satisfactory in transparency, adhesiveness, impact resistance, and flexural fatigue resistance, as shown in the Comparative Examples given later. The reason for this is not fully elucidated. It is presumed that in the interface between the copolymer comprising ethylene as a major component and EVOH, its interfacial adhesive force is high, or its interfacial tension in the molten state is low. These interfacial effects contribute to good transparency, interlayer adhesion, impact resistance, and flexural fatigue resistance. These effects are enhanced when a carboxylic acid-modified polyolefin is used as the compatibilizing agent. According to the present invention, the copolymer (A) preferably has a molecular weight distribution (Mw/Mn) which is not greater than 4. Meeting this requirement leads to good transparency, interlayer adhesiveness, impact resistance, and flexural fatigue resistance. EVOH (B) is an ethylene-vinyl alcohol copolymer having an ethylene content of 20 to 60 mol%, preferably 25 to 55 mol%, most desirably 30 to 50 mol%, and having a degree of hydrolysis (for the vinyl ester moiety) of 95% or above, preferably 98% or above, most desirably 99% or above. In addition, EVOH (B) is not specifically restricted in melting point; however, it preferably has a melting point in the range of 125 to 220°C, preferably 135 to 200°C. With an ethylene content lower than specified above and a melting point higher than specified above, the copolymer is poor in melt-moldability. With an ethylene content higher than specified above, the copolymer is poor in gas barrier properties. With a degree of hydrolysis lower than specified above, the copolymer is poor in gas barrier properties and thermal stability and causes gels and hard spots. It is possible to determine the ethylene content and the degree of hydrolysis by NMR (nuclear magnetic resonance) and to determine the melting point by DSC (differential scanning calorimetry) at a scanning speed of 10°C/min. EVOH used in the present invention preferably has a melt flow rate (MFR) of 0.1 to 100 g/10 min, preferably 0.5 to 50 g/10 min, measured at 210°C under a load of 2,160 g, according to JIS K7210. EVOH is produced using vinyl acetate as a typical vinyl ester. It is also possible to use other fatty acid vinyl esters, such as vinyl propionate and vinyl pivalate. EVOH (B) may contain a vinylsilane compound (as a comonomer) in an amount of 0.0002 to 0.2 mol%. EVOH (B) containing this comonomer has improved melt viscosity, which contributes not only to dispersibility at the time of blending but also to homogeneous coextrusion in the production of multilayered film. Examples of the vinylsilane compound include vinyltrimethoxysilane, vinyltriethoxysilane, vinyltri(β-methoxyethoxy)silane, and γ-methacryloxypropylmethoxysilane, with vinyltrimethoxysilane and vinyltriethoxysilane being particularly preferable. EVOH (B) may also contain a boron compound. EVOH (B) containing a boron compound has improved melt viscosity, which contributes not only to dispersibility at the time of blending but also to homogeneous coextrusion in the production of multilayered film. Examples of the boron compound include boric acids, boric acid esters, boric acid salts, and hydrogenated borons. Boric acids include orthoboric acid, metaboric acid, and tetraboric acid. Boric acid esters include triethyl borate and trimethyl borate. Boric acid salts include alkali metal salts and alkaline earth metal salts of the foregoing boric acids and borax. Of these examples, orthoboric acid (simply referred to as boric acid) and NaBH 4 . The content of the boron compound is 20 to 2,000 ppm, preferably 50 to 1,000 ppm (in terms of boron), so that EVOH (B) gives the ethylene-vinyl alcohol copolymer which experiences a minimum of torque fluctuation at the time of heating and melting. A content lower than 20 ppm is not enough to produce this effect, and a content higher than 2,000 ppm tends to cause gelation and poor molding. EVOH may be copolymerized further with other comonomers such as propylene, butylene, unsaturated carboxylic acid (e.g., (meth)acrylic acid), ester of unsaturated carboxylic acid (e.g., methyl (meth)acrylate and ethyl (meth)acrylate), and vinylpyrrolidone (e.g., N-vinylpyrrolidone), in an amount within which the object of the present invention is not impaired. In the present invention, it is possible to use two or more kinds of EVOH in combination. In addition, it is also possible to incorporate EVOH with a heat stabilizer, UV light absorber, antioxidant, coloring agent, filler, and other resins (e.g., polyamide and partly hydrolyzed ethylene-vinyl acetate copolymer), in an amount within which the object of the present invention is not impaired. According to the present invention, EVOH (B) preferably contains a phosphorus compound in an amount of 2 to 200 ppm, more preferably 3 to 150 ppm, most desirably 5 to 100 ppm, in terms of phosphorus element. A content lower than 2 ppm or higher than 200 ppm will pose a problem with thermal stability and film forming performance (resulting in gel-like hard spots and discoloration after prolonged operation). There are no specific restrictions on the kind of the phosphorus compound to be added to EVOH (B). It is possible to use phosphoric acid, phosphorous acid, and salts thereof. Phosphates may be monobasic phosphate, dibasic phosphate, or tribasic phosphate, and their cations are not specifically restricted. Alkali metal salts and alkaline earth metal salts are preferable. It is desirable to add the phosphorus compound in the form of sodium dihydrogenphosphate, potassium dihydrogenphosphate, disodium hydrogenphosphate, or dipotassium hydrogenphosphate. According to the present invention, EVOH (B) preferably contains an alkali metal salt in an amount of 5 to 5000 ppm in terms of alkali metal element. This alkali metal salt prevents anomalous flow (such as scorching and gum), thereby contributing to scrap recovery and to improvement in impact resistance and flexural fatigue resistance. The content of the alkali metal salt is more preferably 20 to 1000 ppm, most preferably 30 to 500 ppm, in terms of alkali metal element. Examples of the alkali metal include lithium, sodium, and potassium. Examples of the alkali metal salt include monovalent metal salts of aliphatic carboxylic acid, aromatic carboxylic acid, and phosphoric acid, and metal complexes. To be specific, they include sodium acetate, potassium acetate, sodium phosphate, lithium phosphate, sodium stearate, potassium stearate, and sodium ethylenediaminetetraacetae. Of these, sodium acetate, potassium acetate and sodium phosphate are particularly preferable. According to the present invention, the resin composition contains the ethylene-α-olefin copolymer (A) and EVOH (B) such that their ratio (A)/(B) is from 1/99 to 99/1 (by weight). With this blending ratio, the resin composition exhibits the performance intended in the present invention. The resin composition of the present invention is preferably of either of the following two make-ups. According to the first preferred make-up, the resin composition comprises an ethylene copolymer (A) having a density of 0.90 to 0.94 g/cm 3 , EVOH (B), and a carboxylic acid-modified polyolefin (C) and satisfies the following equations (2) and (3): 60/40 ≤ {weight of (A)}/{weight of (B)} ≤ 99/1 0.1/99.9 ≤ X ≤ 20/80 wherein X = {weight of (C)}/{total weight of (A) and (B)}. This resin composition is referred to as resin composition (1) hereinafter. The resin composition (1) has improved melt molding properties, permits effective recycling of regrinds, and provides molded articles (especially multilayered structures) superior in appearance, delamination resistance, transparency, impact resistance, and gas barrier properties. Therefore, it is particularly preferable. The resin composition (1) comprises the ethylene copolymer (A) and EVOH (B) such that their ratio (A)/(B) by weight is from 60/40 to 99/1, preferably from 70/30 to 98/2. With a ratio higher than 99/1, the resin composition is poor in gas barrier properties although it exhibits comparatively good moldability even though the carboxylic acid-modified polyolefin (C) is not added. By contrast, with a ratio lower than 60/40, the resin the composition tends to contain particles of ethylene copolymer (A) and carboxylic acid-modified polyolefin (C) dispersed in EVOH (B). This aggravates the interlayer adhesion. The ethylene copolymer (A) used in the resin composition (1) is a copolymer comprising ethylene as a major component produced by using a single-site catalyst and having a density of 0.90 to 0.94 g/cm 3 . The ethylene copolymer (A) is preferably a copolymer of ethylene with a C 3-8 α-olefin. It is preferably produced in the presence of a single-site catalyst from ethylene in an amount of 80 to 99 wt%, preferably 85 to 98 wt%, more preferably 90 to 97 wt%, and one or more α-olefins in an amount of 1 to 20 wt%, preferably 2 to 15 wt%, more preferably 3 to 10 wt%. The ethylene copolymer (A) used in the resin composition (1) has a density of 0.90 to 0.94 g/cm 3 , preferably 0.905 to 0.935 g/cm 3 , more preferably 0.91 to 0.935 g/cm 3 . With a density higher than 0.94 g/cm 3 , the ethylene copolymer (A) adversely affects the interlayer adhesion and transparency. With a density lower than 0.90 g/cm 3 , the copolymer (A) does not provide elastic modulus necessary for containers to exhibit stiffness for ordinary use. The carboxylic acid-modified polyolefin (C) used in the resin composition (1) is a polyolefin having carboxyl groups in its molecule. It includes, for example, one which is formed by grafting a polyolefin with an unsaturated dicarboxylic acid anhydride and one which is formed by copolymerizing an olefin monomer with an unsaturated carboxylic acid. When added to the ethylene copolymer (A) and EVOH (B), the carboxylic acid-modified polyolefin contributes to compatibility, adhesion strength, and transparency of the composition. The carboxylic acid-modified polyolefin (C) may contain as the olefin moiety ethylene, propylene, 1-butene, 2-butene, and styrene. It may be copolymerized with a monomer such as vinyl acetate and (meth)acrylate ester copolymerized with it. Of these examples, carboxylic acid-modified polyethylene is preferable because of its ability to impart good transparency and compatibility to the resin composition. The unsaturated dicarboxylic acid anhydride used for grafting includes, for example, maleic anhydride, itaconic anhydride, and citraconic anhydride, with maleic anhydride being preferable. The unsaturated carboxylic acid to be copolymerized with olefin monomer includes acrylic acid and methacrylic acid. The carboxylic acid-modified polyolefin (C) has a melt flow rate (MFR) of 0.1 to 100 g/10 min, preferably 0.5 to 50 g/10 min, measured at 190 °C under a load of 2,160 g. The resin composition (1) comprises the ethylene copolymer (A), EVOH (B), and carboxylic acid-modified polyolefin (C) such that the ratio (by weight) of (C)/{(A)+(B)} is 0.1/99.9 to 20/80, preferably 0.5/99.5 to 18/82, more preferably 1/99 to 15/85. With a ratio lower than 0.1/99.9, the resin composition does not exhibit the performance intended in the present invention. With a ratio higher than 20/80, the resin composition is poor in thermal stability (leading to gels and hard spots). The ethylene copolymer (A) and EVOH (B) in the resin composition (1) have melt flow rates Ma and Mb, respectively, such that the ratio Ma/Mb satisfies the following equation (4): 0.05 ≤ Ma/Mb ≤ 5 The requirement is necessary for good dispersibility, melt stability, delamination resistance, and transparency. There are no specific restrictions on the method of blending the ethylene copolymer (A), EVOH (B), and carboxylic acid-modified polyolefin (C). A dry blend of these components may be used as such or preferably after pelletizing by extrusion through a Banbury mixer and single- or twin-screw extruder, followed by drying. This extrusion is preferably carried out at a low temperature using a high-performance extruder, with its hopper sealed with nitrogen, so as to ensure uniform blending (which is necessary to avoid gels and hard spots leading to cracking). A preferred way to achieve better performance is to previously mix (by melting) the ethylene copolymer (A) and/or EVOH (B) with the carboxylic acid-modified polyolefin (C) and then mix this mixture with the ethylene copolymer (A) and/or EVOH (B) and finally mold the resulting blend. Molded articles thus obtained have a good appearance and permit the effective recycling of regrinds. The reason for the improved moldability is not fully elucidated. It is presumed that the mixing of (A) and/or (B) with (C) results in a mixture having their respective characteristics owing to intimate mixing at the molecular level and enhances compatibility between (A) and (B). The consequence is uniform dispersion of the three components and improvement in quality and moldability. The thus obtained resin composition (1) contains the resin components dispersed therein such that particles of (B) and (C) are dispersed in the matrix of (A). Dispersion in this way helps the resin composition to have good transparency and interlayer adhesion. Particles of (B) and (C) dispersed in (A) in the resin composition (1) preferably has an average particle diameter not greater than 5 µm, more preferably not greater than 4 µm, and most desirably not greater than 3 µm. Particles with an average particle diameter larger than 5 µm aggravate the interlayer adhesion and transparency and hence deteriorate the effect of the present invention. Incidentally, the average particle diameter is an arithmetic mean of diameters of particles appearing on an arbitrary cross section. According to the present invention, the resin composition (1) preferably comprises a hydrotalcite compound (D) in an amount of 0.0001 to 2%, more preferably 0.0001 to 1%, based on the total weight of (A) and (B), so as to prevent the occurrence of gels and fisheyes in the layer of the resin composition, thereby ensuring stable operation for a long time. The hydrotalcite compound is particularly a double salt represented by M x Al y (OH) 2x+3y-2z (A) z ·aH 2 O (wherein M denotes Mg, Ca, or Zn; A denotes CO 3 or HPO 4 ; and x, y, z, and a each denotes a positive number). Preferred examples of the hydrotalcite compound are listed below. Mg 6 Al 2 (OH) 16 CO 3 ·4H 2 O Mg 8 Al 2 (OH) 20 CO 3 ·5H 2 O Mg 5 Al 2 (OH) 14 CO 3 ·4H 2 O Mg 10 Al 2 (OH) 22 (CO 3 ) 2 ·4H 2 O Mg 6 Al 2 (OH) 16 HPO 4 ·4H 2 O Ca 6 Al 2 (OH) 16 CO 3 ·4H 2 O Zn 6 Al 6 (OH) 16 CO 3 ·4H 2 O Mg 4.5 Al 2 (OH) 13 CO 3 ·3.5H 2 O Another example of the hydrotalcite compound is a hydrotalcite solid solution disclosed in JP-A-1-308439 (US-A-4,954.557). It is represented by [Mg 0.75 Zn 0.25 ] 0.67 Al 0.33 (OH) 2 (CO 3 ) 0.167 ·0.45H 2 O. According to the present invention, the resin composition (1) preferably further comprises a metal salt of higher aliphatic carboxylic acid (E) in an amount of 0.0001 to 2%, preferably 0.001 to 1%, based on the total weight of (A) and (B), so as to prevent the occurrence of gels and fisheyes in the layer of the resin composition, thereby ensuring stable operation for a long time. The metal salt of higher aliphatic carboxylic acid means a metal salt of C 8-22 higher fatty acid. Examples of the C 8-22 higher fatty acid include lauric acid, stearic acid, and myristic acid. Examples of the metal include sodium, potassium, magnesium, calcium, zinc, barium, and aluminum. Of these metals, alkaline earth metals (such as magnesium, calcium, and barium) are preferable. In a preferred embodiment of the present invention, the resin composition (1) contains both (D) and (E). It is recommended to dilute (D) and (E) 2 to 100 times with an ethylene-α-olefin copolymer produced by using a single-site catalyst before their blending with (A), (B), and (C). This procedure improves their dispersion. The resin composition (1) may be given one or more kinds of hindered phenol or amine heat stabilizer in an amount of 0.01 to 1 wt% of the total weight of (A) and (B), so as to enhance the effect of the present invention. It may also be incorporated with other additives (such as plasticizer, heat stabilizer, UV light absorber, antioxidant, coloring agent, and filler), whose examples are listed below. Antioxidant: 2,5-di-t-butylhydroquinone, 2,6-di-t-butyl-p-cresol, 4,4'-thiobis(6-t-butylphenol), 2,2'-methylene-bis-(4-methyl-6-t-butylphenol), octadecyl-3-(3', 5'-di-t-butyl-4'-hydroxyphenyl)propionate, and 4,4'-thiobis-(6-t-butylphenol). UV light absorber: ethylene-2-cyano-3,3'-diphenyl acrylate. 2-(2'-hydroxy-5'-methylphenyl)benzotriazole, 2-(2'-hydroxy-5'-methylphenyl)benzotriazole, 2-(2'-hydroxy-5'-methylphenyl)benzotriazole, 2-(2'-hydroxy-3'-t-butyl-5'-methylphenyl)-5-chlorobenzotriazole, 2-hydroxy-4-methoxybenzophenone, and 2,2'-dihydroxy-4-methoxybenzophenone. Plasticizer: dimethyl phthalate, diethyl phthalate, dioctyl phthalate, wax, liquid paraffin, and phosphoric acid ester. Antistatic agent: pentaerithrytol monostearate, sorbitan monopalmitate, sulfated polyolefin, polyethylene oxide, and carbowax. Slip agent: ethylene bis-stearamide and butyl stearate. Coloring agent: carbon black, phthalocyanine, quinacridone, indoline, azoic pigment, and red iron oxide. Filler: glass fiber, asbestos, wollastonite, and calcium silicate. The resin composition (1) may be incorporated further with any other polymeric compounds to an extent that the effect of the present invention is not impaired. According to the present invention, it is possible to obtain a multilayered structure superior in appearance and gas barrier properties by laminating a layer of the resin composition (1) and a layer of EVOH having an ethylene content of 20 to 60 mol% and a degree of hydrolysis of 95% or above. Lamination is preferably carried out by coextrusion. It is important that the EVOH used for the multilayered structure has an ethylene content of 20 to 60 mol%, preferably 25 to 55 mol%, and more preferably 30 to 50 mol%. With an ethylene content lower than 20 mol%, the EVOH is poor in melt-moldability. With an ethylene content higher than 60 mol%, the EVOH is poor in gas barrier properties. It is also important that the EVOH has a degree of hydrolysis of 95% or above, preferably 99% or above. EVOH with a degree of hydrolysis lower than 95% is poor in gas barrier properties. The multilayered structure containing the layer of the resin composition (1) may be laminated with inner and/or outer layers of thermoplastic resin for protection of the EVOH layer. The EVOH layer for gas barrier layer is not specifically restricted in thickness. It is usually 5 to 100 µm thick, preferably 10 to 50 µm thick. The layer of the resin composition (1) is usually 10 to 2,000 µm thick, preferably 20 to 1,000 µm thick. The inner and outer layers of thermoplastic resin impart moisture resistance, heat resistance, heat-sealability, and mechanical characteristic to the multilayered structure. They also protect the EVOH layer from moisture which deteriorates its gas barrier properties. The thermoplastic resin is not specifically restricted. It includes, for example, ethylene-α-olefin copolymer (mentioned above), polyethylene, ethylene-vinyl acetate copolymer, ethylene-acrylic acid copolymer, ethylenemethacrylic acid copolymer, ethylene-acrylic ester copolymer, polypropylene, polystyrene resin, polyamide resin, polyester resin, polycarbonate resin, polyurethane resin, and polyvinyl chloride resin. Preferable among these examples are ethylene-α-olefin copolymer, low-density polyethylene, high-density polyethylene, and polypropylene. The most desirable one is ethylene-α-olefin copolymer produced by using a single-site catalyst. These resin layers may contain the above-mentioned additives, such as antioxidant, coloring agent, and filler. The multilayered structure of the present invention may contain an interlayer adhesive resin (AD for short hereinafter). This adhesive resin is not specifically restricted so long as it is capable of bonding layers to each other. It includes, for example, olefin polymer (such as polypropylene and polyethylene), or copolymer of ethylene and a monomer copolymerizable therewith such as vinyl acetate and acrylic ester (such as ethylene-vinyl acetate copolymer, ethylene-methyl (or ethyl) (meth)acrylate copolymer), graft-modified with an unsaturated carboxylic acid and anhydride thereof (such as maleic anhydride) by grafting. A preferred one is the carboxylic acid-modified polyolefin (C) contained in the resin composition. The multilayered structure may be produced by any of extrusion lamination, dry lamination, coinjection molding, coextrusion molding, and solution coating. Coextrusion is preferable because of its easy and economical operation. Coextrusion is divided into coextrusion lamination, coextrusion sheet molding, coextrusion inflation, and coextrusion blow molding. The thus obtained multilayered structure (in the form of sheet, film, and parison) may be reheated and molded into a desired article. Reheating is performed at a temperature not higher than the melting point of the EVOH. Molding is accomplished by drawing (thermoforming) or uniaxial or biaxial stretching (such as roll stretching, pantograph stretching, inflation stretching, and blow molding). The multilayered structure is preferably formed by coextrusion from the resin composition (1) (prepared from components (A), (B), and (C) as mentioned above) and EVOH, so that it has a good appearance and facilitates the recovery of regrinds. The multilayered structure may be irradiated with radiation or electron beams so as to crosslink the layers of EVOH and thermoplastic resin. Alternatively, the raw materials may be incorporated with a chemical crosslinking agent at the time of extrusion. The layers constituting the multilayered structure may have any thickness whose ratio is not specifically restricted. The thickness of the EVOH layer is preferably about 0.5 to 20%, particularly 1 to 10%, of the total thickness. The multilayered structure is not specifically restricted in construction. Typical layer constructions are given below, in which PO stands for polyolefin as the typical thermoplastic resin, AD stands for an adhesive resin and RC(1) stands for the resin composition (1). EVOH/AD/RC(1) EVOH/AD/RC(1)/PO EVOH/AD/RC(1)/AD/PO PO/AD/EVOH/AD/RC(1)/PO RC(1)/AD/EVOH/AD/RC(1)/PO RC(1)/AD/EVOH/AD/PO When having two or more PO layers, the PO layers may be formed from identical or different PO. According to the present invention, the raw material of the resin composition (1) may contain regrinds recovered from said multilayered structure and also scraps recovered from other polyolefin molded articles. Containing EVOH superior in gas barrier properties, the multilayered structure of the above-mentioned layer construction is useful as a packaging material (for foods, medicines, and medical supplies) and industrial material, which need transparency and gas barrier properties. It is of great industrial significance that the resin composition (1) of the present invention permits the recovery and recycling of regrinds from the multilayered structure having polyolefin and EVOH layers and also from the containers made from the multilayered structure. Another preferable resin composition according to the present invention will be explained below. It comprises a copolymer (A) comprising ethylene as a major component and having a density of 0.85 to 0.90 g/cm 3 , and EVOH (B), which satisfies the following equation (5): 1/99 ≤ {weight of (A)}/{weight of (B)} ≤ 40/60 It is referred to as resin composition (2) hereinafter. The resin composition (2) is superior not only in gas barrier properties owing to EVOH as a major component but also in impact resistance and flexural fatigue resistance. The resin composition (2) comprises the copolymer (A) and EVOH (B) in such amounts that their weight ratio (A)/(B) is from 1/99 to 40/60, preferably from 2/98 to 30/70. With a ratio higher than 40/60, the resin composition (2) is poor in gas barrier properties. With a ratio lower than 1/99, the resin composition (2) is poor in impact resistance and flexural fatigue resistance. The ethylene copolymer (A) used in the resin composition (2) is a copolymer comprising ethylene as a major component produced by using a single-site catalyst and having a density of 0.85 to 0.90 g/cm 3 . The ethylene copolymer (A) is preferably a copolymer of ethylene with a C 3-8 α-olefin. It is preferably produced in the presence of a single-site catalyst from ethylene in an amount of 92 to 50 wt%, preferably 90 to 55 wt%, more preferably 85 to 55 wt%, and one or more α-olefins in an amount of 8 to 50 wt%, preferably 10 to 45 wt%, more preferably 15 to 45 wt%. The ethylene copolymer (A) in the resin composition (2) has a density of 0.85 to 0.90 g/cm 3 , preferably 0.855 to 0.895 g/cm 3 , more preferably 0.86 to 0.89 g/cm 3 . With a density higher than 0.90 g/cm 3 , the ethylene copolymer (A) adversely affects impact strength and flexural fatigue resistance. With a density lower than 0.85 g/cm 3 , the copolymer (A) has extremely low crystallinity, which presents difficulties in handling due to chip sticking. The ethylene copolymer (A) and EVOH (B) in the resin composition (2) should have melt flow rates Ma and Mb, respectively, such that the ratio Ma/Mb satisfies the following equation (6) : 0.2 ≤ Ma/Mb ≤ 20 The requirement is necessary for good dispersibility, impact resistance, flexural fatigue resistance, and gas barrier properties. The resin composition (2) may contain, in addition to the ethylene copolymer (A) and EVOH (B), a carboxylic acid-modified polyolefin (C) so that it exhibits good dispersibility, impact resistance, flexural fatigue resistance, and gas barrier properties. The component (C) is identical with that explained above in connection with the resin composition (1). The resin composition (2) preferably comprises the ethylene copolymer (A), EVOH (B), and carboxylic acid-modified polyolefin (C) such that the ratio (by weight) of (C)/{(A)+(B)} is 0.1/99.9 to 20/80, preferably 0.5/99.5 to 15/85, more preferably 1/99 to 10/90. With a ratio lower than 0.1/99.9, the resin composition does not exhibit the performance intended in the present invention. With a ratio higher than 20/80, the resin composition is poor in thermal stability (leading to gels and hard spots). There are no specific restrictions on the method of blending the ethylene copolymer (A), EVOH (B), and modified polyolefin (C). Those methods explained above in connection with the resin composition (1) can be used. The thus obtained resin composition (2) contains the resin components such that particles of the ethylene copolymer (A) are dispersed in the matrix of EVOH (B). Dispersion in this way contributes to good gas barrier properties. The resin composition (2) contains the ethylene copolymer (A) and EVOH (B) in a way that particles of (A) dispersed in (B) have an average particle diameter not greater than 5 µm, preferably not greater than 4 µm, and most desirably not greater than 3 µm. Particles larger than 5 µm aggravate impact resistance and flexural fatigue resistance and hence deteriorate the effect of the present invention. The resin composition (2) may be incorporated with several additives and polymeric compounds, as in the case of the resin composition (1), in order to improve its melt stability and enhance the effect of the present invention. These additive include hydrotalcite compounds, hindered phenol or amine heat stabilizers, and metal salts of higher fatty carboxylic acid (such as calcium stearate and magnesium stearate), which have been explained above in connection with the resin composition (1). The multilayered structure containing the layer of the resin composition (2) may be laminated with inner and/or outer layers of thermoplastic resin for protection of the EVOH layer. The thermoplastic resin for this purpose is not specifically restricted; the same one as explained above in connection with the resin composition (1) may be used. The multilayered structure may contain an interlayer adhesive resin, if necessary. The same one as explained above in connection with the resin composition (1) may be used. The multilayered structure, which contains the layer of the resin composition (2), is not specifically restricted in layer construction. It preferably has a polyolefin (PO) layer of thermoplastic resin and an adhesive resin (AD) layer of carboxylic acid-modified polyolefin. The polyolefin layer contributes to mechanical properties and moisture resistance. Typical examples of layer construction are PO/AD/RC(2) and PO/AD/RC(2)/AD/PO {where RC(2) stands for resin composition(2)}. The layer construction having outer polyolefin layers is desirable because they isolate the layer of the resin composition from moisture. The polyolefin layer may be formed from a polyolefin containing regrinds of EVOH and adhesive resin. The multilayered structure having a layer of the resin composition (2) may be produced in any manner without specific restrictions. It is possible to adopt the above-mentioned method used to produce the multilayered structure having a layer of the resin composition (1). The multilayered structure having a layer of the resin composition (2) is superior in gas barrier properties, impact resistance, and flexural fatigue resistance. Therefore, it is useful as a packaging material (for foods, medicines, and medical supplies) and industrial material, which need these characteristic properties. The resin composition (2) produces its marked effect when used as a bag-in-box container which imperatively need flexibility, especially flexural fatigue resistance. According to a preferred embodiment, the bag-in-box container is made of a laminate having a core layer of the resin composition(2) and inner and outer layers of ethylene-α-olefin copolymer via a layer of adhesive resin. The ethylene-α-olefin copolymer constituting the inner and outer layers is preferably one which has a density of 0.90 to 0.94 g/cm 3 . It may also be one which is produced by using a single-site catalyst or a conventional Ziegler catalyst. It is of great industrial significance that the resin composition (2) of the present invention provides an EVOH composition superior in impact resistance, flexural fatigue resistance, and gas barrier properties, and also provides a multilayered structure having a layer formed from it and a high-performance container made of it. The invention will be described in more detail with reference to the following Examples, which are not intended to restrict the scope of the invention. Examples are divided into two groups, one relating to cups thermoformed from a multilayered sheet and the other relating to a flexible packaging container formed from a multilayered film. Samples were tested by the following methods. • Appearance of multilayered sheet: Samples of multilayered sheet were tested for appearance by visual inspection 30 minutes and 6 hours after the start of operation. Appearance is rated in four grades by the following criterion. A ... no defects in appearance B ... slightly noticeable gels, fisheyes, or streaks C ... moderately noticeable gels, fisheyes, or streaks D ... apparently noticeable gels, fisheyes, or streaks • Particle dispersion in multilayered sheet or film: A specimen cut out of the multilayered sheet or film is dipped in liquid nitrogen and cut at a right angle to the extrusion direction. The cut surface is examined under a scanning electron microscope so as to measure the particle diameter. The result is expressed in terms of arithmetic mean of measurements. • Haze of multilayered sheet: A specimen cut out of the multilayered sheet is coated with silicone oil and measured for haze according to ASTM D1003-61 using HR-100 made by Murakami Shikisai Gijutsu Kenkyusho. • Drop test of thermoformed container: A sample of thermoformed cup is filled with 200 cc of water. The top of the cup is closed by heat sealing with another cup (inverted). The filled cup is dropped on a concrete floor, and the height for the cup to break (allowing water to leak) is recorded. This test is repeated for 30 samples and the results are calculated according to JIS K7211 (Section 8 for calculations) to obtain the height for 50% of the samples to break. • Peel strength of thermoformed container: A specimen (15 mm wide) is cut out of a thermoformed cup (at its flange). The specimen undergoes T-peel test at a peel speed of 250 mm/min. • Oxygen permeability of multilayered film: A specimen cut out of the multilayered film is conditioned at 20°C and 65 %RH and measured for oxygen permeability using an oxygen permeability measuring apparatus (OX-TRAN-10/50A, made by Modern Control Co., Ltd.). The result is expressed in terms of ml/m 2 ·day·atm. • Flexure resistance test of multilayered film: A specimen (12 × 8 inches 30 × 20 cm) is cut out of the multilayered film and conditioned at 20°C and 65 %RH. The specimen is made into a cylinder, 3.5 inches (8.8 cm) in diameter. The cylinder is held by grips at its ends on a Gelbo Flex Tester (made by Rigaku Kogyo). Initially, the grips are 7 inches apart. The specimen is twisted by turning the grips in opposite direction through an angle of 440° such that the distance between the grips is decreased to 3.5 inches (8.8 cm). Then the grips are moved straight and horizontally so that the distance between them is decreased to 2.5 inches (6.3 cm). Finally, the grips are returned to their original positions. (When the specimen is flexed to the utmost limit, the grips are 1 inch (2.5 cm) apart.) These steps are repeated at a rate of 40 cycles per minute. The specimen is observed after 500 cycles each, and the cycles are repeated (up to 10,000 cycles) until pinholes appear in the specimen. This test is carried out at 20°C and 65 %RH. • Drop test of flexible container: A sample of flexible container is prepared by heat sealing from the multilayered film. The sample is filled with water and dropped on a concrete floor. The height for the container to break (allowing water to leak) is recorded. This test is repeated for 30 samples and the results are calculated according to JIS K7211 (Section 8 for calculations) to obtain the height for 50% of the samples to break. Example 1-1 A dry blend was prepared from the following three components. (A) Ethylene-α-olefin copolymer produced by using single-site catalyst, "Affinity FM1570" from Dow Chemical. (80 parts by weight) Comonomer = 1-octene (7.5 wt%) Density = 0.915 g/cm 3 MFR = 1.0 g/10 min (210°C, 2,160 g load) Mw/Mn = 3.6 (B) EVOH (20 parts by weight) Ethylene content = 32 mol% Degree of hydrolysis = 99.6% MFR = 3.1 g/10 min (210°C, 2,160 g load) Content of phosphorus compound (potassium dihydrogenphosphate) = 100 ppm (in terms of phosphorus element) Content of sodium salt (sodium acetate) = 65 ppm (in terms of sodium element) (C) Carboxylic acid-modified polyolefin, "Admer NF500" from Mitsui Petrochemical Industries, Ltd. (low-density polyethylene graft-modified with maleic anhydride). (5 parts by weight) MFR = 3.6 g/10 min (210°C, 2,160 g load) The dry blend was pelletized by extrusion through an extruder (40 mm in diameter, L/D = 24, compression ratio = 3.8) having a Madock-type mixing zone. Thus there was obtained the resin composition(RC) of the present invention. A 6-layered sheet specified below was produced by coextrusion from the resin composition and the above-mentioned three components fed into separate extruders. Layer construction: (A)/(C)/(B)/(C)/(RC)/(A) = 200/25/100/25/450/200 µm Total thickness = 1,000 µm Each component was extruded under the following conditions. Component (A): at 200-240°C through a 65-mm single-screw extruder with an L/D ratio of 22. Component (B): at 170-210°C through a 40-mm single-screw extruder with an L/D ratio of 26. Component (C): at 160-220°C through a 40-mm single-screw extruder with an L/D ratio of 26. Resin composition: at 160-210°C through a 40-mm single-screw extruder with an L/D ratio of 22. The melt was discharged from a feed block die (600 mm wide) at 240°C. The extruded sheet was observed 30 minutes and 6 hours after the start of operation. A sample taken 30 minutes after the start of operation was found to have a haze of 35%. Observation of the cross section of the sheet under a scanning electron microscope revealed that the matrix of the ethylene-α-olefin copolymer (A) contains dispersed therein particles (1.5 µm in average diameter) of the EVOH (B) and the carboxylic acid-modified polyolefin (C). The resulting sheet was made into cups by thermoforming under the following conditions. Thermoforming machine: made by Asano Seisakusho Sheet temperature: 170° C Mold: 70 mm in diameter, 70 mm long Draw ratio: S = 1.0 Air pressure: 5 kg/cm 2 Plug: 45 mm in diameter, 65 mm long, syntax form Plug temperature: 150°C Mold temperature: 70°C The resulting cups underwent drop test. Samples did no break when dropped from a height under 1.7 meters. The peel strength of the flange of the cup was 2.0 kg/15 mm wide (which is sufficient for practical use). The results of evaluation are shown in Tables 1 and 2. Example 1-2 A 5-layered sheet specified below was produced by coextrusion from the same three components (A), (B), and (C) as used in Example 1-1, which were fed into separate extruders. Layer construction: (A)/(C)/(B)/(C)/(A) = 400/25/200/25/400 µm This multilayered sheet was reground, and the resulting regrinds were used in place of the resin composition in repeating the procedure of Example 1-1. Samples of the sheets and cups were evaluated in the same manner as mentioned above. The results of evaluation are shown in Tables 1 and 2. Examples 1-3, 1-4, 1-10 and 1-16 and Comparative Examples 1-1, 1-3 and 1-4 The same procedure as in Example 1-1 was repeated except that the ethylene-α-olefin copolymer (A) was replaced by any of the following products. The results are shown in Tables 1 and 2. Incidentally, "Affinity" is a product from Dow Chemical produced by using a single-site catalyst, and others are products produced by using a conventional Ziegler catalyst. Example 1-16 and Comparative Example 1-4 gave cups which are not sufficient in stiffness to retain their forms. Example 1-3: "Affinity PL1845" from Dow Chemical copolymer containing 9.5 wt% 1-octene, density = 0.910 g/cm 3 MFR = 3.5 g/10 min (210°C, 2,160 g load) Mw/Mn = 3.3 Example 1-4: "Affinity HF1030" from Dow Chemical copolymer containing 2.0 wt% 1-octene, density = 0.935 g/cm 3 MFR = 2.5 g/10 min (210°C, 2,160 g load) Mw/Mn = 3.8 Example 1-10: "Affinity SM1350" from Dow Chemical copolymer containing 9.5 wt% 1-octene, density = 0.913 g/cm 3 MFR = 30 g/10 min (210°C, 2,160 g load) Mw/Mn = 3.7 Example 1-16: "Affinity PF1140" from Dow Chemical copolymer containing 15 wt% 1-octene, density = 0.895 g/cm 3 MFR = 1.6 g/10 min (210°C, 2,160 g load) Mw/Mn = 3.6 Comparative Example 1-1: LLDPE "UF420" from Mitsubishi Chemical Corporation copolymer containing 4.95 wt% 1-hexene, density = 0.925 g/cm 3 MFR = 0.8 g/10 min (210°C, 2,160 g load) Mw/Mn = 7.5 Comparative Example 1-3: HDPE "Nipolon Hard" from Tosoh Corporation density = 0.953 g/cm 3 MFR = 1.0 g/10 min (210°C, 2,160 g load) Mw/Mn = 6.8 Comparative Example 1-4: "Esprene N0372" from Sumitomo Chemical Co., Ltd. copolymer containing 13 wt% 1-butene, density = 0.89 g/cm 3 MFR = 3.0 g/10 min (210°C, 2,160 g load) Mw/Mn = 4.6 Examples 1-5, 1-6, 1-7, 1-8 and 1-11 The same procedure as in Example 1-1 was repeated except the EVOH (B) was replaced by any of the following products. The results are shown in Tables 1 and 2. Example 1-5: EVOH Ethylene content = 27 mol% Degree of hydrolysis = 99.6% MFR = 3.9 g/10 min (210°C, 2,160 g load) Content of phosphorus compound (potassium dihydrogenphosphate) = 100 ppm (in terms of phosphorus element) Content of sodium salt (sodium acetate) = 65 ppm (in terms of sodium element) Example 1-6: EVOH Ethylene content = 44 mol% Degree of hydrolysis = 99.7% MFR = 3.5 g/10 min (210°C, 2,160 g load) Content of phosphorus compound (potassium dihydrogenphosphate) = 100 ppm (in terms of phosphorus element) Content of sodium salt (sodium acetate) = 65 ppm (in terms of sodium element) Example 1-7: EVOH Ethylene content = 32 mol% Degree of hydrolysis = 99.6% MFR = 3.1 g/10 min (210°C, 2,160 g load) Content of phosphorus compound = 0 ppm Content of sodium salt (sodium acetate) = 65 ppm (in terms of sodium element) Example 1-8: EVOH Ethylene content = 32 mol% Degree of hydrolysis = 99.6% MFR = 3.1 g/10 min (210°C, 2,160 g load) Content of phosphorus compound (potassium dihydrogenphosphate) = 100 ppm (in terms of phosphorus element) Content of sodium salt (sodium acetate) = 3 ppm (in terms of sodium element) Example 1-11: EVOH Ethylene content = 32 mol% Degree of hydrolysis = 99.6% MFR = 33 g/10 min (210°C, 2,160 g load) Content of phosphorus compound (potassium dihydrogenphosphate) = 100 ppm (in terms of phosphorus element) Content of sodium salt (sodium acetate) = 65 ppm (in terms of sodium element) Comparative Example 1-2 The same procedure as in Example 1-2 was repeated except that the ethylene-α-olefin copolymer (A) (which was produced by using a single-site catalyst and used for production of the pellets of the resin composition) was replaced by LLDPE ("UF420" from Mitsubishi Chemical Corporation which was produced by using a conventional Ziegler catalyst) specified below. copolymer containing 4.95 wt% 1-hexene density = 0.925 g/cm 3 MFR = 0.8 g/10 min (210°C, 2,160 g load) Mw/Mn = 7.5 The results are shown in Tables 1 and 2. Example 1-9 The same procedure as in Example 1-1 was repeated except that the carboxylic acid-modified polyolefin (C) was "Admer QF500" (from Mitsui Petrochemical Industries, Ltd.) specified below in place of "Admer NF500" (from Mitsui Petrochemical Industries, Ltd.). Polypropylene graft-modified with maleic anhydride, MFR = 3.0 g/10 min (230°C, 2,160 g load). The results are shown in Tables 1 and 2. Examples 1-17, 1-18 and 1-19 The same procedure as in Example 1-1 was repeated except that mixing ratio of the components (A), (B), and (C) was changed as follows. Example 1-17: (A):(B):(C) = 80:20:0 Example 1-18: (A):(B):(C) = 50:50:5 Example 1-19: (A):(B):(C) = 80:20:30 Comparative Examples 1-5, 1-6 and 1-7 The same procedure as in Comparative Example 1-1 was repeated except that mixing ratio of the components (A), (B), and (C) was changed as follows. Comparative Example 1-5: (A):(B):(C) = 80:20:0 Comparative Example 1-6: (A):(B):(C) = 50:50:5 Comparative Example 1-7: (A):(B):(C) = 80:20:30 Examples 1-12, 1-14 and 1-15 The same procedure as in Example 1-1 was repeated except that the dry blend of the components (A), (B), and (C) was incorporated with the following compounds. Example 1-12: hydrotalcite {Mg 4.5 Al 2 (OH) 13 CO 3 ·3.5H 2 O}, 0.1 part by weight. Example 1-14: magnesium stearate, 0.1 part by weight. Example 1-15: hydrotalcite {Mg 4.5 Al 2 (OH) 13 CO 3 ·3.5H 2 O}, 0.1 part by weight; and magnesium stearate, 0.1 part by weight. Example 1-13 The same procedure as in Example 1-1 was repeated except that the ethylene-α-olefin copolymer (A) was replaced by a mixture comprising 80 parts by weight of the same ethylene-α-olefin copolymer (A) as used in Example 1-1 end 0.1 part by weight of hydrotalcite {Mg 4.5 Al 2 (OH) 13 CO 3 ·3.5H 2 O}. The two components were dry-blended and pelletized by extrusion through a 40-mm extruder (L/D = 24, compression ratio = 3.8) equipped with a Madock-type mixing zone. The results are shown in Tables 1 and 2. Example 2-1 A dry blend was prepared from the following two components. (A) Ethylene-α-olefin copolymer produced by using single-site catalyst, "Engage EG8100" from Dow Chemical. (10 parts by weight) Comonomer = 1-octene (24 wt%) Density = 0.87 g/cm 3 MFR = 1.0 g/10 min (210°C, 2,160 g load) Mw/Mn = 3.7 (C) Carboxylic acid-modified polyolefin, "Admer NF500" from Mitsui Petrochemical Industries, Ltd. (LLDPE graft-modified with maleic anhydride). (5 parts by weight) MFR = 3.6 g/10 min (210°C, 2,160 g load) The dry blend was pelletized by extrusion through an extruder (40 mm in diameter, L/D = 24, compression ratio = 3.8) having a Madock-type mixing zone. Thus there was obtained the resin composition (pellets) of the present invention. Then, 15 parts by weight of the resin composition was mixed with 90 parts by weight of EVOH (B) specified below by extrusion under the same conditions as above. Ethylene content = 32 mol% Degree of hydrolysis = 99.6% MFR = 3.1 g/10 min (210°C, 2,160 g load) Content of phosphorus compound (potassium dihydrogenphosphate) = 100 ppm (in terms of phosphorus element) Content of potassium = 125 ppm (in terms of potassium element) Content of sodium salt (sodium acetate) = 65 ppm (in terms of sodium element) Thus there was obtained the desired resin composition comprising three resin components. A 5-layered film specified below was produced by coextrusion from the resin composition and the following two components fed into separate extruders. Layer construction: LLDPE/AD/RC/AD/LLDPE = 50/5/20/5/50 µm Total thickness = 130 µm LLDPE: Ethylene-α-olefin copolymer produced by using a conventional Ziegler catalyst ("US420" from Mitsubishi Chemical Corporation) density = 0.925 g/cm 3 MFR = 0.8 g/10 min (210°C, 2,160 g load) AD: Linear low-density polyethylene graft-modified with maleic anhydride for the adhesive resin layer ("Admer NF500" from Mitsui Petrohemical Industries, Ltd.) MFR = 3.6 g/10 min (210°C, 2,160 g load) Each component was extruded under the following conditions. LLDPE: at 200 to 240°C through a 65-mm single-screw extruder with an L/D ratio of 22. AD: at 160 to 220°C through a 40-mm single-screw extruder with an L/D ratio of 26. Resin composition: at 200 to 240°C through a 40-mm single-screw extruder with an L/D ratio of 26. The melt was discharged from a feed block die (600 mm wide) at 240°C. A sample of the resulting multilayered film was cooled with liquid nitrogen and its cross section was observed under a scanning electron microscope. It was found that the EVOH (B) contains particles of the ethylene-α-olefin copolymer (A) and the carboxylic acid-modified polyolefin (C) dispersed therein and having an average particle diameter of 1.6 µm (arithmetic mean). After conditioning at 20°C and 65 %RH, the multilayered film was tested for oxygen permeability using OX-TRAN-10/50A made by Modern Control. A specimen (12 × 8 inches 30 × 20 cm) was cut out of the multilayered film and conditioned at 20°C and 65 %RH. The specimen was made into a cylinder, 3.5 inches in diameter. The cylinder was held by grips at its ends on a Gelbo Flex Tester (made by Rigaku Kogyo). Initially, the grips were 7 inches apart. The specimen was twisted by turning the grips in opposite direction through an angle of 440° such that the distance between the grips was decreased to 3.5 inches. Then the grips were moved straight and horizontally so that the distance between them was decreased to 2.5 inches. Finally, the grips were returned to their original positions. (When the specimen was flexed to the utmost limit, the grips were 1 inch apart.) These steps were repeated at a rate of 40 cycles per minute. The specimen was observed after 500 cycles each, and the cycles were repeated (up to 10,000 cycles) until pinholes appeared in the specimen. This test was carried out at 20°C and 65 %RH. A sample of flexible container was prepared by heat sealing from the multilayered film. (Two sheets of film measuring 20 by 30 cm were placed one over the other and three sides were heat-sealed, with the 20-cm side left open.) This sample was filled with water (20°C) and the open side was heat-sealed. In this way there was obtained a flexible container for bag-in-box. This container was dropped on a concrete floor. The height for the container to break (allowing water to leak) was recorded. This test was repeated for 30 samples and the results were calculated according to JIS K7211 (Section 8 for calculations) to obtain the height for 50% of the samples to break. The results are shown in Table 3. Comparative Example 2-1 The procedure of Example 2-1 was repeated to produce film and flexible container except that the layer of the resin composition was replace by the one formed from only the same EVOH as used in Example 2-1. The results are shown in Table 3. Examples 2-2, 2-3 and 2-4 The procedure of Example 2-1 was repeated to prepare the resin composition (pellets) from the ethylene-α-olefin copolymer (A) and EVOH (B) except that their mixing ratio (A)/(B) by weight was changed to 5/95 (in Example 2-2), 20/80 (in Example 2-3), and 50/50 (in Example 2-4). Using this resin composition, films and flexible containers were prepared in the same manner as in Example 2-1. The results are shown in Table 3. Examples 2-5 and 2-6 The same procedure as in Example 2-1 was repeated except the EVOH (B) was replaced by any of the following products. The results are shown in Table 3. Example 2-5: EVOH Ethylene content = 27 mol% Degree of hydrolysis = 99.6% MFR = 3.9 g/10 min (210°C, 2,160 g load) Content of phosphorus compound (potassium dihydrogenphosphate) = 100 ppm (in terms of phosphorus element) Content of potassium = 125 ppm (in terms of potassium element) Content of sodium salt (sodium acetate) = 65 ppm (in terms of sodium element) Example 2-6: EVOH Ethylene content = 44 mol% Degree of hydrolysis = 99.7% MFR = 3.5 g/10 min (210°C, 2,160 g load) Content of phosphorus compound (potassium dihydrogenphosphate) = 100 ppm (in terms of phosphorus element) Content of potassium = 125 ppm (in terms of potassium element) Content of sodium salt (sodium acetate) = 65 ppm (in terms of sodium element) Example 2-7 and 2-8 and Comparative Examples 2-2 to 2-4 The same procedure as in Example 2-1 was repeated except that the ethylene-α-olefin copolymer (A) was replaced by any of the following products. Incidentally, the resins used in Example 2-7 and 2-8 are those which are produced by using a single-site catalyst, and the resins used in Comparative Examples 2-2 to 2-4 are those which are produced by using a conventional Ziegler catalyst. The results are shown in Table 3. Example 2-7: "Engage CL8003" from Dow Chemical copolymer containing 18 wt% 1-octene, density = 0.885 g/cm 3 MFR = 1.0 g/10 min (210°C, 2,160 g load) Mw/Mn = 3.4 Example 2-8: "Engage FM1570" from Dow Chemical ethylene-α-olefin copolymer containing 7.5 wt% 1-octene, density = 0.915 g/cm 3 MFR = 1.0 g/10 min (210°C, 2,160 g load) Mw/Mn = 3.6 Comparative Example 2-2: "Esprene N0372" from Sumitomo Chemical Co., Ltd. copolymer containing 13 wt% 1-butene, density = 0.89 g/cm 3 MFR = 3.0 g/10 min (210°C, 2,160 g load) Mw/Mn = 4.6 Comparative Example 2-3: "V0111" from Sumitomo Chemical ethylene-propylene copolymer containing 22 wt% propylene, density = 0.87 g/cm 3 MFR = 0.9 g/10 min (210°C, 2,160 g load) Mw/Mn = 4.3 Comparative Example 2-4: "UF420" from Mitsubishi Chemical Corporation ethylene-α-olefin copolymer containing 4.95 wt% 1-hexene, density = 0.925 g/cm 3 MFR = 0.8 g/10 min (210°C, 2,160 g load) Mw/Mn = 7.5 Example 2-9 and 2-10 The same procedure as in Example 2-1 was repeated except that the ethylene-α-olefin copolymer (A) and EVOH (B) were replaced by any of the following products. Incidentally, the ratio of Ma/Mb was 0.03 (in Example 2-9) and 23.1 (in Example 2-10), wherein Ma stands for MFR of the ethylene-α-olefin copolymer (A) and Mb stands for MFR of the EVOH (B). The results are shown in Table 3. • Example 2-9 (A) : ethylene-α-olefin copolymer (the same one as used in Example 2-1. (B) : EVOH Ethylene content = 32 mol% Degree of hydrolysis = 99.6% MFR = 33 g/10 min (210°C, 2,160 g load) Content of phosphorus compound (potassium dihydrogenphosphate) = 100 ppm (in terms of phosphorus element) Content of potassium = 125 ppm (in terms of potassium element) Content of sodium salt (sodium acetate) = 65 ppm (in terms of sodium element) • Example 2-10 (A) : "Engage SM1250" from Dow Chemical which was produced by using a single-site catalyst copolymer containing 19 wt% 1-octene, density = 0.885 g/cm 3 MFR = 30 g/10 min (210°C, 2,160 g load) Mw/Mn = 3.5 (B) : EVOH Ethylene content = 32 mol% Degree of hydrolysis = 99.6% MFR = 3.1 g/10 min (210°C, 2,160 g load) Content of phosphorus compound (potassium dihydrogenphosphate) = 100 ppm (in terms of phosphorus element) Content of sodium salt (sodium acetate) = 65 ppm (in terms of sodium element) Example 2-11 The same procedure as in Example 2-1 was repeated except that the ethylene-α-olefin copolymer (A), EVOH (B), and carboxylic acid-modified polyolefin (C) were dry-blended and they were extruded all at once. The results are shown in Table 3. Example 2-12 The same procedure as in Example 2-1 was repeated except that the ethylene-α-olefin copolymer (A) and EVOH (B) were extruded all at once, excluding the carboxylic acid-modified polyolefin (C). The results are shown in Table 3. Comparative Example 2-5 The same procedure as in Comparative Example 2-2 was repeated except that the ethylene-α-olefin copolymer (A) and EVOH (B) were extruded all at once, excluding the carboxylic acid-modified polyolefin (C). The results are shown in Table 3. The present invention provides a resin composition which is superior in melt moldability, gas barrier properties, flexural fatigue resistance, and impact resistance. This resin composition can be used for a layer of multilayered structure to impart a good appearance, transparency, impact resistance, delamination resistance, gas barrier properties and flexural fatigue resistance.

Claims: A resin composition which comprises a copolymer (A) comprising ethylene as a major component produced by using a single-site catalyst, and an ethylene-vinyl alcohol copolymer (B) having an ethylene content of 20 to 60 mol% and a degree of hydrolysis of 95% or above, said resin composition satisfying the following equation (1): 1/99 ≤ {weight of (A)}/{weight of (B)} ≤ 99/1 The resin composition as defined in Claim 1, wherein the copolymer (A) is an ethylene-α-olefin copolymer in which the α-olefin has 3 to 8 carbon atoms. The resin composition as defined in Claim 1 or 2, wherein the copolymer (A) has a molecular weight distribution (Mw/Mn) of not greater than 4. The resin composition as defined in any of Claims 1 to 3, wherein the ethylene-vinyl alcohol copolymer (B) contains a phosphorus compound in an amount of 2 to 200 ppm in terms of phosphorus element. The resin composition as defined in any of Claims 1 to 4, wherein the copolymer (A) has a density of 0.90 to 0.94 g/cm 3 and the resin composition further comprises a carboxylic acid-modified polyolefin (C) and satisfies the following equations (2) and (3): 60/40 ≤ {weight of (A)}/{weight of (B)} ≤ 99/1 0.1/99.9 ≤ X ≤ 20/80 wherein X = {weight of (C)}/{total weight of (A) and (B)}. The resin composition as defined in Claim 5, wherein resin particles comprising the ethylene-vinyl alcohol copolymer (B) and the carboxylic acid-modified polyolefin (C) are dispersed in a matrix of the copolymer (A), and have an average particle diameter not greater than 5 µm. The resin composition as defined in Claim 5 or 6, wherein the melt flow rate Ma of the copolymer (A) and the melt flow rate Mb of the ethylene-vinyl alcohol copolymer (B) satisfy the following equation (4): 0.05 ≤ Ma/Mb ≤ 5 The resin composition as defined in any of Claims 5 to 7, which further comprises a hydrotalcite compound (D) in an amount of 0.0001 to 2% based on the total weight of (A) and (B). The resin composition as defined in any of Claims 5 to 8, which further comprises a metal salt of a higher aliphatic carboxylic acid (E) in an amount of 0.0001 to 2% based on the total weight of (A) and (B). A multilayered structure which comprises a layer of the resin composition as defined in any of Claims 5 to 9, and a layer of an ethylene-vinyl alcohol copolymer having an ethylene content of 20 to 60 mol% and a degree of hydrolysis of 95% or above. The multilayered structure as defined in Claim 10, which further comprises at least one layer comprising an ethylene-α-olefin copolymer produced by using a single-site catalyst and having a density of 0.90 to 0.94 g/cm 3 , in which the α-olefin has 3 to 8 carbon atoms, and at least one layer comprising a carboxylic acid-modified polyolefin. The multilayered structure as defined in Claim 10 or 11, which is formed by coextrusion. The resin composition as defined in any of Claims 1 to 4, wherein the copolymer (A) has a density of 0.85 to 0.90 g/cm 3 , and the resin composition satisfies the following equation (5): 1/99 ≤ {weight of (A)}/{weight of (B)} ≤ 40/60 The resin composition as defined in Claim 13, wherein the melt flow rate Ma of the copolymer (A) and the melt flow rate Mb of the ethylene-vinyl alcohol copolymer (B) satisfy the following equation (6): 0.2 ≤ Ma/Mb ≤ 20 The resin composition as defined in Claim 13 or 14, which further comprises a carboxylic acid-modified polyolefin (C) and satisfies the following equation (7): 0.1/99.9 ≤ X ≤ 20/80 wherein X = {weight of (C)}/{total weight of (A) and (B)}. A multilayered structure which comprises a layer of the resin composition as defined in any of Claims 13 to 15, a layer of adhesive resin, and a layer of polyolefin. A bag-in-box container comprising the multilayered structure as defined in Claim 16, wherein a core layer of the resin composition is laminated with inner and outer layers of an ethylene-α-olefin copolymer via layers of adhesive resin.

Inventors: NAKATSUKASA SHIGEKI, OHGI HIROYUKI, YOSHIMI KAZUYORI, NAKATSUKASA, SHIGEKI, OHGI, HIROYUKI, YOSHIMI, KAZUYORI
Applicants: KURARAY CO, KURARAY CO., LTD.
Application year: 1997
Main classification: C08L23
IPC codes: C08L23