Heat resistant container

Abstract: The present invention provides a heat-resistant container comprising an ethylene-vinyl alcohol copolymer layer and a cystalline polyester layer. In particular, when an ethylene-vinyl alcohol copolymer containing a drying agent is used, the obtained container is both ovenable and retortable, thereby being highly useful.

Description: This invention relates to a heat-resistant plastic container which can undergo retort treatment and has a high gas barrier property, thereby protecting food contained therein from putrefaction or oxidation even during storage at room temperature and being excellent in capability for a long-term storage, and which at the same time can undergo heating in a microwave or in an electric cooking oven while containing food without transferring the content into a different container. Recently, as the home use of electric cooking ovens as well as microwaves is being wide-spread, requirements for plastic containers to be usable in the both ovens ("dual-ovenable") have been enhanced. As resins usable in electric cooking oven (220°C),e.g. crystalline polyester (hereinafter referred to as PET) and polyetherimide are known; and in particular, containers utilizing crystalline PET have been put to practical use. However, conventional PET containers cannot, since they are lacking both in retortability (capability for retort treatment) and in gas barrier property, be used for containers for transporting and storing foods at room temperature, and their uses therefore have been limited. Multi-layer containers made of polypropylene and a gas-barrier resin have been used for containers being capable of retort treatment and having gas barrier properties. As such gas-barrier resins, ethylene-vinyl alcohol copolymer (hereinafter referred to as EVOH) or polyvinylidene chloride resins have been used. However, multi-layer containers utilizing polypropylene have, though usable in microwaves, no heat resistance against electric cooking ovens. US-A-4,425,410 discloses a retortable multi-layer structure comprising an EVOH layer containing a drying agent and a polyolefin layer provided thereon, but does not mention a crystalline PET layer on an EVOH layer containing a drying agent. JP-A-62660/1984 discloses an ovenable container comprising a crystalline PET, but does not mention a container comprising a crystalline PET layer and an EVOH layer or an EVOH layer containing a drying agent provided thereon. EP-A-0 249 051 discloses a composition comprising a matrix of an ethylene-vinyl alcohol copolymer having dispersed therein a drying agent in a particulate state. The volume-area average diameter of the grains of the drying agent having a long diameter of not less than 10µm is not greater than 30µm. A multi-layer structure comprises layers of such a composition. Gas barrier property of the multi-layer structure is hardly reduced after a retort treatment and thus, the multi-layer structure is extremely useful for packaging of food, expecially packaging of retorted food. This application relates to prior art according to Art. 54 (3) EPC. Then, it is thought to improve food storing capability of the heat-resistant container utilizing crystalline (crystallized) PET by combining with the PET an EVOH to get a multi-layer container. In fact, a multi-layer container obtained by co-extruding a crystalline PET, an EVOH and an adhesive resin into a sheet, followed by deep blowing, has a high degree of gas barrier property, and is excellent in performances of protecting food from oxidation. However, it has been noted that the obtained container shows, when subjected to a retort treatment with hot water at a temperature of 120°C, a decrease in its gas barrier property due to water absorption by the EVOH layer. A test was made to use a polyvinylidene chloride instead of EVOH, but the molding was not successful due to a poor thermal stability. A heat-resistant container provided with both capability for retort treatment and a gas barrier property has thus not been known. The object underlying the invention is to get a heat-resistant container having both retortability and storage capability as represented by gas barrier property. The present invention provides a heat-resistant container comprising an ethylene-vinyl alcohol copolymer layer and a polyester resin layer, characterized in that said polyester resin layer comprises a crystalline polyester resin comprising a thermoplastic polyester and a polyolefin as crystallization accelerator. The container shows excellent storing capability incorporating retortability, as well as an excellent dimensional stability when heated in an electric cooking oven or in a microwave. The multi-layer container of the present invention is excellent in gas barrier property and in retortability, and further in heat resistance, thereby enabling a long-term storage of food, as well as enabling boiling or heating in a microwave and in an electric oven (220°C) without transferring the contents beforehand to a different container. The container is useful also in the field where maintaining of an odor is required. The crystalline PET as used in the present invention is a composition comprising a thermoplastic polyester containing as a principal component at least 80 mol%, preferably at least 90 mol% of ethylene terephthalate units, and a crystallization accelerator incorporated therein. The PET resin may contain a dicarboxylic acid(s) other than terephthalic acid or a glycol component(s) other than ethylene glycol. Relative to the molecular weight of the polyester, the inherent viscosity is preferably at least 0.60 dl/g, more preferably at least 0.70 dl/g, since the molecular weight greatly influences the sheet moldability and the properties of the obtained container. The inherent viscosity as used herein means a viscosity value measured in a mixed solvent of phenol/tetrachloroethane (1:1 by weight) at 30°C. The crystallization accelerator is selected from polyolefins, particularly polymers obtained from olefin monomers having 2 to 6 carbon atoms such as low density polyethylene, high density polyethylenes, linear low density polyethylene, polypropylene, polyisopropylene, polybutene and poly-4-methylpentene. They are used in an amount from 1 to 15% by weight, preferably from 2 to 8% by weight. Addition of 0.05 to 5% by weight of a heat stabilizer to the PET is effective since the finished products are exposed to high temperatures for a long time. One or more heat stabilizers shown below are often used. Examples of the heat stabilizers include alkylated substituted phenols, bisphenols, substituted bisphenols, thiobisphenols, polyphenols, thiobisacrylates, aromatic amines, organic phosphites and polyphosphites. Examples of the aromatic amines are primary polyamines, diarylamines, bisdiarylamines, alkylated diarylamines, ketone-diarylamine condensation products, aldehyde-amine condensation products and aldehyde-amine. Particularly preferred heat stabilizers are polyphenols having at least two phenol ring structures therein, such as tetrakis {methylene-3-(3,5-di-t-butyl-4-hydroxydiphenyl)-propionate} methane and 1,3,5-trimethyl-2,4,6-tris(3,5-di-t-butyl-4-hydroxybenzyl) benzene, of the two the former being more preferred. Further in mixing the above compounds, other additives including a plasticizer, a lubricant, an antistatic agent, and in particular, a dye may optionally incorporated within the range not to impair the effect and function of the present invention. Further, in order to obtain a foamed structure or a three-dimensional structure, there may as required also be used various CO₂ generators, cross-linking agents and auxiliary agents. It is important to disperse uniformly in the PET the above-mentioned crystallization accelerator, heat stabilizer, and other additives, since the uniformity greatly affects the performances of the finished container. There is no particular limit to the methods employed for adding and uniformly dispersing the additives, and examples of the methods include a process which comprises incorporating the additives such as crystallization accelerator during the polymerization of the PET; a process which comprises adding the PET in a desired percentage to master pellets obtained by dry blending the PET with the additives, and then melt-extruding the blend composition, followed by pelletization; a process which comprises directly using a pelletized resin obtained by dry blending the PET with the additives and then melt-extruding the blend, followed by pelletization; and a process which comprises dry blending the PET with the additives and directly using the blend composition. Preferably used is the process which comprises incorporating the additives during the polymerization of the PET and the process which comprises directly using a pelletized resin obtained by dry blending the PET with the additives, and then melt-extruding the blend composition, followed by pelletization. Adjustment for the inherent viscosity of the obtained PET composition is made such that the viscosity as measured in a mixed solvent of phenol/tetrachlorethane (1:1 by weight) at 30°C will be from 0.65 to 1.2 dl/g, preferably from 0.70 to 1.0 dl/g, and sometimes as occasions demand the adjustment is done by using a conventional solid-phase polymerization to increase the viscosity. Optionally, there may be incorporated in the aforementioned crystalline PET a compound having crosslinking group(s) such as a several functional carboxylic and/or hydroxyl group (three or more functional groups) in an amount of from 0.005 to 2 mol%. Where such a crystalline PET having crosslinking groups is used (in addition to the advantage in that even if the thickness of an EVOH layer is made large or if deep blowing is done, there does not occur any uneven elongation, breakage or irregularities in the gas barrier properties) molding is possible at a sheet temperature at thermoforming of as low as from 110 to 120°C, thereby suppressing a draw down caused by a high temperature heating which has been a big problem at thermoforming (130 to 150°C) of polyester sheets, and also variations in container thickness resulting therefrom. Examples of the compounds having several functional carboxylic groups or several functional hydroxylic groups include trimellitic acid, pyromellitic acid pyromellitic acid dianhydride, 1,2,3-propanetricarboxylic acid and 1,2,3,4-benzenetetracarboxylic acid; or pentaerythritol, trimethylolethane, trimethylolpropane, trimethylolhexane, 1,3,5-trimethylolbenzene, glycerol and sorbitol. These compounds may be used alone or in admixtures of more than two. Among the above particularly preferred are pentaerythritol and trimethylol propane. The content of the compound having several functional group is from 0.005 to 2 mol%, preferably from 0.01 to 1 mol%. EVOH as used herein includes any saponified products of ethylene-vinyl acetate copolymers, among which particularly suited for the object of the present invention are those containing from 25 to 60 mol% of ethylene units, and having a saponification degree of the vinyl acetate units of at least 96%, preferably at least 99%, and a melt index (190°C, 2160 g) of from 0.2 to 60 g/10 min. Further EVOH referred to in the present invention may be those modified with a copolymerizable monomer in a range of not greater than 5 mol%. Example of such monomers for modification include propylene, 1-butene, 1-hexene, 4-methyl-1-pentene, acrylic acid esters, methacrylic acid esters, maleic acid, fumaric acid, itaconic acid, higher fatty acid vinyl esters, alkylvinyl ethers, N-(2-dimethylaminoethyl) methacrylamides or quaternized products thereof, N-vinylimidazole or quaternized products thereof, N-vinylpyrrolidone, N-n-butoxymethylacrylamide, vinyltrimethoxysilane, vinylmethyldimethoxysilane and vinyldimethylmethoxysilane. As the EVOH matrix, two or more EVOH resins having a different composition can also be mixed and used as a mixture. Further additives, for example, coloring agents such as pigments and dyes, antistatic agents, UV absorbants, plasticizers, heat stabilizers and lubricants can be incorporated in the matrix within such a range that does not impair the effects of the present invention. Further as the drying agent referred to in the present invention, there are suitable salts capable of forming hydrates, namely, salts which absorb water in the form of crystal water, in particular, phosphates such as sodium dihydrogenphosphate, sodium monohydrogenphosphate, sodium phosphate, lithium phosphate and sodium pyrophosphate. Particularly anhydrides thereof are most suited for the present invention in view of the effects. Other hydrate-forming salts, for example, salts such as sodium borate and sodium sulfate, and particularly anhydrides thereof are also suited for the present invention. Further other hygroscopic compounds, for example, sodium chloride, sodium nitrate, sugar, silica gel, bentonite, molecular sieve and highly water-absorbent resins may also be used. These drying agents can also be used in admixture of two or more simultaneously. In the present invention, it is necessary that the drying agent be dispersed in the matrix of EVOH as fine grains and the drying agent grains have a volume-area average diameter of not greater than 30 µm, preferably 25 µm or less, most preferably 20 µm or less, in the grains having a long diameter of 10 µm or more. By forming such a fine dispersion state, the multi-layer structure having a high gas permeability resistance that has not been hitherto achieved, can be obtained. The composition having such a fine dispersion state can be obtained only by careful combination of particular processings suited for the purpose. First, it is desired to pay special attention to the drying agent in such a manner that the drying agent having a grain diameter as fine as possible be given upon precipitation from an aqueous solution of the salts through e.g. spray drying. The drying agent grains can be classified into 30 µm or less, preferably 10 µm or less and then provided for use but, in general, the salts dried are subjected to pulverization using a jet mill, an impact mill, a ball mill or a vibration ball mill. The ground grains are classified into ultrafine grains of 30 µm or less, preferably 10 µm or less, using a classification machine such as an air classification machine, The 30 µm or less as used herein means that the grains exceeding 30 µm are less than 0.01 % in the volume fraction, namely, the fine grains of 30 µm or less are present in an amount of at least 99.9 %. The graininess of the ultrafine grains is a value determined by the Coulter counter method. Upon the measurement of the graininess, the grains are preliminarily sieved through a sieve having a mesh of 10 to 75 µm, if necessary, in order to condense a small amount of coarse grains and, the coarse grains of the sieve is analyzed by the Coulter counter method so that the coarse grains can be analyzed with high accuracy. Next, the ultrafine grains of the drying agent described above are mixed with EVOH. For mixing, there are a method for mixing the fine grains of the drying agent with powders, grains or pellets of EVOH using a conventional mixer, for example, a Henschel mixer, a super mixer or a tumbling mixer; a method which comprises mixing the fine grains of the drying agent with a melt of EVOH to make a master batch and mixing the master batch with powders, grains, pellets or melts of EVOH. Then, the mixture is kneaded at temperatures higher than the melting point of EVOH to prepare the composition. EVOH and the drying agent grains may also be directly fed in a kneader to effect kneading, without preliminary mixing of EVOH and the drying agent grains as described above. Upon this kneading operation, the fine grains of the drying agent tend to be aggregated with each other; even if ultrafine grains of 10 µm or less are used, the remarkable effects of the present invention cannot be obtained if the fine grains are agglomerated and the agglomerates exceeding the volume-area average diameter set in the present invention are formed. Accordingly, the kneading operation is extremely important in the present invention. As the kneader to give the composition having a high dispersion state, there are most suited continuous twin rotor kneaders such as a continous intensive mixer,or a kneading type twin screw extruder (same directions or different direction), but, there may also be used batch type twin rotor extruders such as a Banbury mixer, an intensive mixer or a pressure kneader. Further as another continuous mixing devices, there may also be used rotary disks having an attrition mechanism such as a stone mill, e.g., KCK kneader Extruder manufactured by KCK Co., Ltd. Among kneaders conventionally used, there are a single screw kneader equipped with a kneading part (Dulmage, CTM, etc.) or handy type kneaders such as a Brabender mixer; in the case of using such kneaders, however, it is difficult to obtain the excellent composition of the present invention. Of these kneaders, the most preferred kneader for the purposes of the present invention is a continuous intensive mixer. Commercially available models are FCM manufactured by Farrel Co., Ltd., CIM manufactured by The Japan Steel Works, Ltd., KCM, NCM, LCM or ACM manufactured by Kobe Steel Works, Ltd. From a practical standpoint, it is preferred that a device equipped with a kneader having mounted a single screw extruder beneath the kneader be adopted to perform kneading and extrusion pelletization simultaneously. For the kneading purpose of the present invention, there may also be used a twin screw kneading extruder having kneading disks or kneading rotors, for example, TEX manufactured by The Japan Steel Works, Ltd., ZSK manufactured by Werner & Pfleiderer Co., Ltd., TEM manufactrued by Toshiba Machine Co., Ltd. or PCM manufactured by Ikegai Iron Works, Inc. In using these continuous kneaders, the shape of a rotor or disk plays an important role. In particular, a gap (tip clearance) between a mixing chamber and a rotor tip or a disk top is important; if the gap is too narrow or two wide, the composition having good dispersion of the present invention cannot be obtained. It is most suited that the tip clearance be in the range of 1 to 5 mm. In order to obtain the composition having good dispersion of the present invention, it has been found that kneading should be made in a unit work of the kneader of at least 0.1 kwh/kg, preferably 0.2 to 0.8 kwh/kg. The unit work is determined by dividing energy (quantity of electric power consumed; kw) used for the kneading by an amount (kg) of the kneading treatment per an hour and its unit is kwh/kg. In order to produce the composition of the present invention, it is required that the kneading be performed at a unit work value higher than that adopted for conventional kneading. To render the unit work at least 0.1 kwh/kg, it is insufficient to merely increase the rotation number of a kneader but it is preferred to cool the composition during kneading with a jacket, thereby to lower the temperature and increase the viscosity. If the kneading is conducted in such a state that the viscosity is low, it is difficult to obtain the composition contemplated in the present invention. Therefore, it is effective to conduct the kneading at a kneading temperature ranging from the melting point of EVOH to a temperature higher than the melting point by 60 °C, more preferably ranging from the melting point of EVOH to a temperature higher than the melting point by 40 °C, at a discharged resin temperature in an outlet of a kneading part. It is desired that the rotation number of a rotor of the kneader be in the range of 100 to 1200 rpm, preferably 200 to 1200 rpm, more preferably 400 to 1200 rpm. The inner diameter of the chamber in the kneader is generally 30 mm or more, preferably in the range of 50 to 400 mm (D). It is preferred that L/D of the kneader be 4 to 10. Further the kneader may be single or two or more kneaders combined together may also be used. The longer the kneading time, the better the results; in view of thermal deterioration or change of EVOH or from an economic standpoint, however, the kneading time is generally in the range of 10 to 600 seconds, preferably 20 to 200 seconds, most preferably 20 to 100 seconds. There is no particular restriction to the ratio of EVOH to the drying agent used but the ratio of 97 : 3 to 50 : 50, particularly 95 : 5 to 70 : 30, by weight, is preferred. Measurement of the graininess of the drying agent grain in the composition is made by the microscopic method; in general, the graininess is determined by visual observation or an image analysis device with respect to a photography of the grains. In the present invention, it is required that among the dispersed grains, the volume-area average diameter of the grains having a long diameter of 10 µm or more is not greater than 30 µm. The long diameter as used herein means a distance between two parallel lines which give the longest distance when a projected image of each grain is inserted between the parallel lines. Regarding the grains having a long diameter of 10 µm or more, an average grain diameter must be determined. Various methods are known to determine the average grain diameter; a convenient method suited for the purpose of the present invention is that an average value D of a long diameter L and a diameter B in the direction rectangular to L is rendered an average diameter. This method is one of the methods often adopted by those skilled in the art. Thus, when its average diameter D N is determined with respect to N pieces of grains in an appropriate measurement range (200 µm × 200 µm), its volume-area average diameter D AV is defined as follows: D AV = Σ D N ³/Σ D N ² As has been made clear in the present invention, the volume-area average diameter of the grains having a long diameter of at least 10 µm, among the drying agent grains in the composition of the present invention, greatly affects the gas permeability resistance of the multi-layer structure comprising this composition as a layer(s). The reason is not necessarily clear but it is assumed that grains having a large grain diameter would be particularly disadvantageous for a hygroscopic effect or gas permeability resistance of EVOH. As the adhesive resin used in the present invention, any adhesive resin for PET and EVOH may be used, but choice should be made taking into consideration retortability and capability of electric cooking oven heating. Most preferred is a modified polyester comprising a dicarboxylic component and a glycol component, which contains one or more of Al, Cr, Sn, Ge and Si in an amount of from 0.1 to 5 moles against 100 moles of the dicarboxylic acid unit. Among the elements, Al and Cr are, since they give large bond strengths, preferred, and Al is particularly preferred. Regarding the content of the element, where the content is less than 0.1 mole, the effect is not fully produced; on the other hand a content exceeding 5 moles will cause unfavorable phenomena such as gelation of the polymer and coloring. It is preferred that these elements be present in the polyester not as admixture therewith but in a state chemically bonded thereto which state gives a higher bond strength. An example of methods for chemically bonding these elements to the polyester molecule is a process which comprises adding a compound of the aforementioned element (particularly preferred is a metal ester, chelate compound or organic acid salt) at the time of polymerisation of the polyester and conducting polymerization, Examples of Al compounds include aluminum acetylacetonate, aluminum ethoxide, aluminum propoxide and reaction products of these compound with a monocarboxylic acid; examples of Cr compounds include chromium acetylacetonate and chromium monocarbonates; examples of Sn compounds include tetraethyl stannate, tetrapropyl stannate, tetrabutyl stannate and reaction products of a monocarboxylic acid therewith; examples of Ge compounds include germanium dioxide; examples of Si compounds include methyltrimethoxysilane, methyltriethoxysilane, dimethyldimethoxysilane and diphenyldimethoxysilane. Particularly preferred are aluminum acetylacetonate, aluminum ethoxide and aluminum propoxide. These compounds are incorporated into a polyester polymerization system after near completion of the polyester polymerization and at below 230°C. They are added in a shape dissolved into a diol or dissolved into a monocarboxylic acid or its ester to prevent gelation of polymers during the polymerization. Examples of the dicarboxylic acid component to constitute the polyester used as the adhesive resin in the present invention are aromatic dicarboxylic acids such as terephthalic acid, isophthalic acid, orthophthalic acid, naphthalenedicarboxylic acid, diphenyletherdicarboxylic acid and diphenyl-4,4'-dicarboxylic acid; aliphatic carboxylic acids such as oxalic acid, malonic acid, succinic acid, glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid and sebacic acid; and alicyclic acids such as cyclohexanedicarboxylic acid. One, two or more than two of these compounds can be used. Examples of the glycol components include aliphatic glycols such as ethylene glycol, 1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,9-nonanediol, diethylene glycol and triethylene glycol; and alicyclic diols such as cyclohexanediol and cyclohexanedimethanol; and they are used alone or in combinations of more than two. Further a small amount of a tri-or more functional carboxylic acid or alcohol can optionally be used. Preferred dicarboxylic acids are terephthalic acid, isophthalic acid and adipic acid; while preferred diols are ethylene glycol and diethylene glycol. The inherent viscosity of the obtained polyester is preferably at least 0.50 dl/g, more preferably at least 0.60 dl/g. The inherent viscosity herein is measured in a phenol/tetrachloroethane mixed solvent (1:1 in weight ratio) at 30°C. As other adhesive resins used in this invention, mentions are made of a polyesteramide copolymer having a molar ratio of ester group/amide group of from 90/10 to 10/90. Examples of the dicarboxylic acid component to constitute the copolymer are aromatic dicarboxylic acids such as terephthalic acid, isophthalic acid, orthophthalic acid, naphthalenedicarboxylic acid, diphenyletherdicarboxylic acid and diphenyl-4,4'-dicarboxylic acid; aliphatic dicarboxylic acids such as oxalic acid, malonic acid, succinic acid, glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid and sebacic acid; and alicyclic acids such as cyclohexanedicarboxylic acid. One or more than two of these compounds can be used. Examples of the glycol components include aliphatic glycols such as ethylene glycol, 1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, diethylene glycol and triethylene glycol; and alicyclic diols such as cyclohexanediol and cyclohexanedimethanol; and they are used alone or in combinations of two or more. Further a small amount of a tri-or more functional carboxylic acid or alcohol can optionally be used. Examples of the amine components include piperazine; diamines such as pentaethylenediamine, hexaethylenediamine, nonaethylenediamine, decaethylenediamine, undecaethylenediamine and nonadecaethylenediamine; acid amides such as lauro lactam, undecaneamide, hexamethylenesebacamide, hexamethyleneadipamide, ω-aminoheptanoic acid and ω-aminononanoic acid. Also used are melt-blended compositions of the above-mentioned copolymer with a polyester or a polyamide, and further blended compositions of a polyester with a polyamide. Where the ester group and the amide group is present in at least 90%, the adhesion between the heat resistant PET and EVOH is insufficient for use. Molar ratios of ester group/amide group of from 85/15 to 15/85 are preferably used. Preferably used is a poly(ester-amide) comprising at least one compound each selected from: terephthalic acid, adipic acid, azelaic acid and succinic acid as a dicarboxylic acid component, ethylene glycol and 1,4-cyclohexanedimethanol as a glycol component, and piperazine as an amide component, the content of piperazine being from 30 to 90 mol% based on total moles of piperazine and the glycol component(s); or a composition of a polyester comprising at least one compound selected from: terephthalic acid, adipic acid, azelaic acid and succinic acid as a dicarboxylic acid component; and ethylene glycol and 1,4-cyclohexanedimethanol as a glycol component, and 6 nylon, 6-66 nylon, 66 nylon, 6-12 nylon or 6-9 nylon melt-blended with the above polyester in an amount of from 10 to 80% by weight. In the present invention, there is employed as a method for producing the heat-resistant multi-layer container, a process which comprises getting a multi-layer sheet or parison of the EVOH composition and the crystalline PET with the adhesive resin inbetween by extrusion lamination, dry lamination, co-extrusion lamination, co-extrusion sheet preparation (feed block process or multi-manifold process) co-extrusion direct blowing, co-extrusion piping, co-injection or various solution coatings; but there is also a process of directly producing the molded container. Where a container is obtained by the direct producing process, the obtained container is heat-treated in a mold heated to a temperature sufficiently high for achieving a desired crystallization degree, thereby acquiring heat resistance. The temperature of the mold is in a range of from 150 to 215°C, preferably from 160 to 200°C; and the container is kept in the mold for 2 to 60 seconds, preferably for 2 to 20 seconds. On the other hand, where the container is obtained from a multi-layer sheet or parison by a secondary processing, it is important to rapidly cool the multi-layer sheet or parison just after the molding, in order to minimize the growth of crystallization generated after the molding. The obtained multi-layer sheet or parison (hereinafter referred to as "multi-layer structure") is thermoformed by heating as rapidly as possible, the thermoforming temperature being in a range of from 110 to 170°C, preferably from 120 to 160°C. There is no particular limit to the moisture content of the EVOH constituting the multi-layer structure when it is thermoformed, but the moisture content is preferably lower than from 0.01 to 5%. The thus thermoformed container is heat-treated in a mold heated to a temperature sufficiently high for achieving the desired crystallization degree, thereby getting heat resistance. The temperature of the mold is in a range of from 150 to 215°C, preferably from 160 to 200°C; and the container is kept in the mold for 2 to 60 seconds, preferably for 2 to 20 seconds. Since the molded article is heated to a high temperature and is therefore soft, special attention should be paid when taking it out of the mold, and as occasions demand reputting it into a cooled mold or blowing cold air into the mold is performed to straighten the shape. The thus molded article has a shrinkage ratio at the container body (longitudinal direction) of less than 10%, preferably less than 6% when heated in an electric cooking oven at 220°C for 30 minutes. The shrinkage ratio at the container body (longitudinal direction) herein is a value represented by: 100 X (size before heating - size after heating )/size before heating. There are no particular limits either to the shape of the molded articles of the multi-layer structure. They may be shaped to a tray, cup or bottle. The drawing ratio for processing secondarily the multi-layer structure into a molded article is not more than 20 times in area ratio, preferably from 3 to 15 times. Scraps or wastes formed upon trimming when obtaining the molded article are granulated and thereafter directly, or after being pelletized, recovered for use. The recovery methods are not particularly limited, but include, after granulation, a process which comprises drying the granules if they have absorbed moisture and then dry blending the granule with the raw material PET; a process which comprises pelletizing the granulated scrap, and thereafter dry blending with the raw material PET; and a process which comprises blend-pelletizing the raw material PET with the granulated scrap. The ratio of blending the scrap with the raw material PET composition is normally from about 2 to 100%. It is often preferred, when recovering the scrap, to add at least one compound selected of metal soaps (e.g. aliphatic and/or aromatic carboxylic acid salt), chelate compounds (e.g. EDTA), and alkali metal salts or alkali earth metal salts of carboxylic acids. Representative examples for the construction of the multilayer structure are crystalline PET/EVOH composition/crystalline PET, crystalline PET/adhesive resin/EVOH composition/adhesive resin/crystalline PET, crystalline PET/adhesive resin/EVOH composition/adhesive resin/crystalline PET/PET, crystalline PET/adhesive resin/EVOH composition/adhesive resin/PET, PET/crystalline PET/adhesive resin/EVOH composition/adhesive resin/crystalline PET/PET, crystalline PET/recovery/adhesive resin/EVOH composition/adhesive resin/crystalline PET, crystalline PET/recovery/adhesive resin/EVOH composition/adhesive resin/recovery/crystalline PET, crystalline PET/recovery/adhesive resin/EVOH composition/adhesive resin/crystalline PET/PET and PET/crystalline PET/recovery/adhesive resin/EVOH composition/adhesive resin/crystalline PET. Among the above constructions, one with EVOH composition layer provided on its both surface crystalline PET layers via addhesive resin layers is preferred. Instead of PET, other heat-resistant resins such as polyamide, polyetherimide, polysulfone, polyphthalatecarbonate and polycarbonate may also be used. The thickness of the construction is not particularly limited; but generally, the total thickness of the container body is from 200 µm to 2000 µm, while the thickness of the EVOH layer is from 2 µm to 200 µm and that of the adhesive resin layer is from 2 µm to 200 µm. The thus obtained multi-layer container of the present invention is a food container having an excellent gas barrier property and an excellent heat resistance, which is capable of storing foods for a long period at room temperature, as well as heatable as it is, without transferring the food contained to another container, by boiling, in a microwave and in an electric cooking oven (200°C). In particular, containers utilizing the EVOH composition incorporating a drying agent of the present invention exhibit an excellent effect in that there hardly occurs the deformation or delamination of the containers when they are heated in an electric cooking oven or in a microwave. The reason for this is estimated to lie in an unexpected fact that the heat resistance of EVOH composition remarkably increases when the composition incorporates a drying agent. The container is also useful in the field where odor-retaining property is required. Next, another embodiment of the present invention is described below. While, as stated before, the container comprising an EVOH layer incorporating a drying agent and a crystalline PET layer(s) provided on at least one surface of the EVOH layer is best in that it is retortable and ovenable, the container comprising an EVOH layer not incorporating any drying agent and a crystalline PET layer(s) provided on at least one surface of the EVOH layer can also undergo heating in a microwave or an electric cooking oven. Though this container decreases, as also stated before, when subjected to a retort treatment, its gas barrier property caused by moisture absorption by the EVOH, it has a high heat resistance. Further, by selecting a proper interlayer adhesive resin, for example the afore-mentioned polyester-related adhesive, between the EVOH layer and a crystalline PET layer, there can be obtained a container which suffers no interlayer delamination and has an excellent shock resistance, and besides, produces no coloring of the adhesive resin or odor generation. The container thus obtained is also excellent in dimensional stability, the shrinkage ratio at the container body (longitudinal direction) when heated in an electric cooking oven at 220°C for 30 minutes being not more than 10%; and in particular, exhibits a great performance when the construction is crystalline PET/adhesive resin/EVOH/adhesive resin/crystalline PET. Also effective is a construction crystalline PET/adhesive resin/EVOH/adhesive resin if required/other thermoplastic resin having a melting point of at least 200°C. As the other thermoplastic resin having a melting point of at least 200°C used herein, a resin having a melting point of at least 220°C and a high moisture permeability such as polyamide or polycarbonate is preferred. These containers can well withstand heating in an electric cooking oven, which will be apparent from Examples 15 through 26 described herein later. Hereinbelow the present invention will be explained in more detail by reference to Examples. In the Examples "parts" means parts by weight. EXAMPLES Example 1 Ultrapulverization and classification of anhydrous sodium monohydrogenphosphate was performed using a jet pulverizer (MICRON JET MJ-3, made by Hosokawa Micron Co.) and a pneumatic classifier (MICRON SEPARATOR, made by the same company). After dispersing the raw material powder in methanol, observation was made with a loupe to find that there are contained a number of particles having diameters of at least 500 µm and having an average particle diameter (median diameter) as determined with a Coulter Counter of 86 µm. Similarly, fine powder after the ultrapulverization gave a maximum particle diameter (with Coulter Counter) of 13 µm and a median diameter of 6.4 µm (powders having particle diameter of at least 13 µm was contained in an amount less than 0.1%). 20 parts of the thus obtained anhydrous sodium monohydrogenphosphate and 80 parts of EVOH [content of ethylene unit: 32 mol%, melt index measured at 190°C under a load of 2160 g: 1.3 g/10 min, and melting point (primary exotherm temperature on DSC; scanning speed: 10°C/min): 181°C] were mixed with each other first preliminary in a Henschel Mixer and thereafter by high speed mixing to obtain a mixture. After that, the mixture was subjected to blend-extrusion-pelletization in a 2-stage twin-screw different-direction continuous kneader with the mixing chamber having an inner diameter of 54 mm (D), L/D = 5.8 (first stage) and L/D = 4.2 (second stage) (LCM-50, made by Kobe Steel Works, Ltd.) and a single-screw extruder connected therewith, to give pellets of the composition (EVOH Composition 1). The operation was conducted with a rotor having a chip clearance between the mixing chamber of 3 mm; a kneading temperature (at the outlet) of from 206 to 220°C, a kneading time of from 30 to 40 seconds, a rotor rotation of from 530 to 650 rpm and a unit work of from 0.3 to 0.6 kwh/kg. The thus obtained pellets were pressed in a hot press at 220°C to give a thin film having a thickness of about 100 µm. Observation on the thin film was made with an optical microscope for state of dispersion of powders. A photograph of magnification 800 was taken. This was done by setting the magnification of the microscope at 50 to increase the depth of focus, and by succeedingly enlarging to a total magnification of 800 times. The average diameter of particles having long diameters of at least 10 µm was determined which then calculated the volume-area average diameter of 17.6 µm. As crystalline PET was used a polyester composition obtained by dry blending 100 parts of an unmodified polyethylene terephthalate having an inherent viscosity of 0.90 dl/g with 3 parts of a low density polyethylene having a MI (190°C, 2160 g) of 5.0 g/10 min, 1.2 parts of TiO₂ as a pigment and 0.5 part of Irganox 1010 (made by Ciba-Geigy) as a heat stabilizer, and thereafter pelletizing the composition with a 40-⊘ extruder of twin-screw and vent type, followed by drying at 150°C for 8 hours. As the adhesive resin, a polyester resin obtained by the following method was used. A polymerization tank equipped with a nitrogen gas inlet, a stirrer and a cooling pipe was charged with 64 parts of bis-β-hydroxyethyl terephthalate, 36.5 parts of adipic acid, 15.5 parts of ethylene glycol, 14.9 parts of diethylene glycol and 0.04 part of antimonium trioxide, followed by reaction at 200°C for 4 hours. The resulting reaction solution was added with an organic aluminum compound separately prepared in an amount converted to aluminum atom of 0.08 part and 0.02 part of tributyl phosphate, and the mixture was first heated to 250°C and, while gradually depressurizing, further to 270°C, followed by polymerization under a reduced pressure of 0.1 mmHg for 90 minutes, to give a resin. The inherent viscosity of the resin was 0.1 dl/g and the glass transition temperature was -5°C. A co-extrusion was conducted using a co-extrusion sheet forming machine having 3 extruders, a 3 kind/5 layer feed block and a take-up, to obtain a multi-layer structured sheet having a construction of crystalline PET/adhesive resin/EVOH Composition 1/adhesive resin/crystalline PET (thicknesses: 900/50/100/50/900 µm). The obtained sheet was thermoformed with a vacuum pressure forming machine (made by Asano Machine Works Ltd.) to give a cup-shape container (opening diameter: 72 mm, bottom diameter: 65 mm, and height: 35 mm). The thermoforming was, conducted under conditions of draw forming a sheet at 130°C and then heat-setting in a mold at 180°C for 10 seconds. The obtained container had a good appearance. When the empty container was heated in an electric cooking oven at 220°C for 20 minutes, the shrinkage ratio (longitudinal size change of the container) was less than 3%, and the container showed a good appearance and no deformation or delamination. The thus thermoformed container was filled with water, and thereafter heatsealed with a stopper of a multi-layer film comprising an aluminum foil (60 µm) and a polyester sealant resin layer (15 µm) laminated on the aluminum foil. The thus sealed containers were then heat-treated with hot water at 120°C for three periods of 30 minutes, 60 minutes and 120 minutes using a retorting apparatus (high temperature and high pressure cooking sterilization tester, RCS-40RTGN, made by Hisaka Seisakusho Co.), followed by storage in a testing room with an atmosphere of 20°C and 65% RH. After storing 6 months, the oxygen concentrations in the containers were measured. The results are shown in Table 1. The oxygen concentrations of the containers of the present invention were all less than 5 ppm, which are sufficiently good for storing foods. One of the remaining thermoformed containers was filled with meat sauce, heatsealed and retorted for 60 minutes in the same manner as above, followed by storage for 6 months in an atmosphere of 20°C and 65% RH. After the storage, the container was opened. The meat sauce showed no discoloration and tasted good. Portions of the cup container before retorting were cut out, and heated in xylene at 120°C to remove crystalline PET and adhesive resin by dissolution, to give films of the EVOH composition in the container. The obtained films were observed with an optical microscope for state of dispersion of powders. Photographs of magnification 800 were taken. This was done by setting the magnification of the microscope at 50 to increase the depth of focus, and by succeedingly enlarging to a total magnification of 800 times. From the photographs, average diameters of particles having long diameters of at least 10 µm present in a region measuring 200 µm x 200 µm each on 10 separately positioned specimens on the container wall, were measured, followed by calculation of a volume-area average diameter to be 17.7 µm. Separately, the co-extrusion molding, thermoforming and retorting of Example 1 was repeated by using, instead of EVOH Composition 1 described in Example 1, the EVOH which was also described in Example 1. After an storage over 6 months, the oxygen concentration was measured. The results are also shown in Table 1. The concentrations measured are about 5 times those obtained on EVOH Composition 1. The container was filled with meat sauce, retorted for 60 minutes and thereafter stored for 6 months. After the storage the container was opened. The meat sauce showed, though slightly, a discoloration. Intermediate layer Oxygen concentration in the cup (after 6 month, ppm) Retorted for: 30 min 60 min 120 min Example 1 Composition 1 2.0 3.6 4.4 EVOH 10.3 15.1 18.6 Examples 2 through 10 Ultrapulverization of various drying agents was conducted. The obtained fine powders were used instead of the anhydrous sodium monohydrogenphosphate powder of Example 1, kneaded and extruded with the EVOH (of Example 1) to give pellets of corresponding compositions. The pellets were co-extrusion molded and then thermoformed into cups. The obtained cups were retorted and thereafter stored for 6 months. The oxygen concentrations in the cups after the storage were measured, and the intermediate layers of the cups were taken out for observation with a microscope, from which the volume-area average diameter (D av ) each was calculated for the dispersed drying agent particles having long diameters of at least 10 µm. The results are shown in Table 2. The storing capabilities of the compositions of the present invention, particularly the compositions utilizing drying agents of Examples 2 through 5 were remarkably high, and were sufficient for storing various types of food. In Examples 6 and 7, or 8 through 10, the cups exhibited remarkable storing capability when retorted for 30 minutes. This time is sufficient for a variety of foods; however, they show some tendency to decrease in storing capabilities when retorted as long as 120 minutes. Separately, the obtained empty cups were heated in an electric cooking oven for 20 minutes. After the heating the cups still had good appearances and showed no delamination. Example 11 Example 1 was repeated except for replacing low density polyethylene by polypropylene, which are crystallization accelerators. The obtained container was good, showed a shrinkage ratio after being heated at 220°C in an electric cooking oven of 4%, and showed also a good appearance after the heating. The container was filled with meat sauce, retorted for 60 minutes, and stored for 6 months. After the storage the container was opened. The meat sauce showed no discoloration and tasted good. Example 12 Example 1 was repeated except for increasing the incorporation amount of the crystallization accelerator from 3% by weight to 6% by weight. The obtained container was good, showed a shrinkage ratio after being heated at 220°C in an electric cooking oven of 4%, and showed a good appearance after the heating. The container also passed the test for storing capability using meat sauce. Example 13 Example 1 was repeated except for replacing the adhesive resin by a poly(ester-amide) having an inherent viscosity of 0.75 dl/g comprising a copolyester (1,4-cyclohexanedimethyl/azelate = 9/50 by mole) modified with 41 mol% of piperadine. The then molar ratio of ester group/amide group was 18/22. The obtained container was good, showed a shrinkage ratio after being heated at 220°C in an electric cooking oven of 4%, which was good. The container also passed the test for storing capability using meat sauce. Example 14 Example 1 was repeated except for replacing the adhesive resin by pellets of a resin obtained by blending 100 parts of a copolyester (ethylene/isophthalate/terephthalate) modified with 35 mol% of isophthalic acid, having an inherent viscosity of 0.75 dl/g, with 80 parts of 6-66 nylon, followed by pelletization using a 40-⊘ twin-screw vent-type extruder and drying at 150°C for 8 hours. The then molar ratio of ester group/amide group was 60/40. The obtained container was good, showed a shrinkage ratio after being heated at 220°C in an electric cooking oven of 3.5%, which was good. The heat-treated container showed only slight discoloration in its appearance, which was no problem for practical use. The container also passed the test for storing capability using meat sauce. Example 15 An EVOH having a melt index (MI; 190°C, 2160 g) of 1.6 g/10 min comprising 44 mol% of ethylene having a saponification degree of 99.4% incorporating 0.02 mol% of vinyltrimethoxysilane was used as EVOH component. As the heat-resistant crystalline PET was used a polyester composition obtained by dry blending 100 parts of an unmodified polyethylene terephthalate having an inherent viscosity of 0.90 dl/g with 3 parts of a low density polyethylene having a MI (190°C, 2160 g) of 5.0 g/10 min, 1.2 parts of TiO₂ as a pigment and 0.5 part of Irganox 1010 (made by Ciba-Geigy) as a heat stabilizer, and thereafter pelletizing the composition with a 40-⊘ extruder of twin-screw and vent type, followed by drying at 150°C for 8 hours. As adhesive resin, a polyester resin obtained by the following method was used. A polymerization apparatus comprising a 300-ml three-neck flask equipped with a nitrogen gas inlet, a stirrer and a cooling pipe was charged with 64 g of bis-β-hydroxyethyl terephthalate, 36.5 g of adipic acid, 15.5 g of ethylene glycol, 14.9 g of diethylene glycol and 40 mg of antimonium trioxide, followed by reaction at 200°C for 4 hours. The resulting reaction solution was added with an aluminum compound in an amount converted to aluminum atom of 0.52 mole to 100 moles of dicarboxylic acid component, which aluminum compound had been obtained by reacting 200 ml of hexylene glycol with 0.20 mole of aluminum isopropoxide, 0.10 mole of capric acid, 0.30 mole of p-oxybenzoic acid and 0.20 mole of acetylacetone, at 100°C; and further added with 25 µl of tributyl phosphate; and the mixture was first heated to 250°C and, while gradually depressurizing, further to 270°C, followed by polymerization at the temperature under a reduced pressure of 0.1 mmHg for 90 minutes, to give a resin. The inherent viscosity of the resin was 0.61 dl/g and the glass transition temperature was -5°C. A co-extrusion was conducted using a 3 kind/5 layer co-extruder to obtain a sheet. The construction of the obtained sheet is as shown in Table 3. The obtained sheet was thermoformed with a vacuum pressure forming machine equipped with a round-cup mold at the sheet temperature of 130°C and at a drawing ratio of 1. The obtained cup was heat set at the mold temperature of 180°C for 10 seconds. The obtained container had a good appearance. When the container was heated in an electric cooking oven at 220°C for 20 minutes, the shrinkage ratio (longitudinal) was 3%, the shrinkage ratio being a value calculated by the formula: 100 x (size before heating - size after heating)/size before heating . The container after the heating showed a good appearance. The gas barrier property of the EVOH layer of the container was measured at 20°C-65% RH with TYPE 10/50 made by Mocon Company to give 1.8 cc·20 µm/m²·24 hr·atm before the heating and 1.7 cc·20 µm/m²·24 hr·atm after the heating, both of which are excellent. The container before heating was filled with salad oil and heatsealed on the top with a 100-µm biaxially drawn PET film laminated thereon with a sealant. The container was then dropped onto concrete floor at 20°C to measure the dropping impact strength (height dropped).The height from which 5 containers from a total of 10 were dropped was at least 1.5 m, which proves a high resistance to dropping shock. The height dropped at -20°C was 1 m. The containers were sterilized by boiling at 80°C for 2 hours and by steam sterilization at 121°C for 30 minutes separately, and thereafter allowed to stand for 3 days at 20°C, 65% RH. Then the caps of the containers were opened and the containers were heated in a microwave for 5 minutes. Both containers showed good appearances. The then temperature of salad oil was 180°C. They also showed good appearances when they were heated in an electric cooking oven at 220°C for 30 minutes. Further, the containers, one boiled and the other steam sterilized, were opened and removed of the salad oil, and thereafter the empty containers were heated in an electric cooking oven at 220°C for 30 minutes. Both show no delamination or deformation, and they had good appearances. The gas barrier properties of the containers were measured at 20°C-65% RH to give all nearly the same value of 1.8 cc·20 µm/m²·24 hr·atm, which is excellent. Example 16 Example 15 was repeated except for using an EVOH comprising 32 mol% of ethylene and having a saponification degree of 99.6% and MI (190°C, 2160 g) of 1.6 g/10 min, the EVOH not containing Si. The results are shown in Table 3. Example 17 Example 15 was repeated except for using an EVOH comprising 32 mol% of ethylene and having a saponification degree of 99.4% and MI (190°C, 2160 g) of 1.6 g/10 min, the EVOH incorporating 0.3 mol% of vinyltrimethoxysilane, changing the thickness of the intermediate EVOH layer to 15 µm , and further changing the adhesive resin to one obtained by the following process: The same polymerization apparatus used in Example 15 was charged with 64 g of bis-β-hydroxyethyl terephthalate, 4.6 g of isophthalic acid, 24 g of sebacic acid, 30 g of ethylene glycol, and 40 mg of antimony trioxide, followed by reaction at 200°C for 4 hours. The resulting reaction solution was added with the same aluminum compound used in Example 15 in an amount converted to aluminum atom of 0.52 mole to 100 moles of dicarboxylic acid component, and further added with 25 µl of tributyl phosphate; and the mixture was first heated to 250°C and, while gradually depressurizing, further to 270°C, followed by polymerization at the temperature under a reduced pressure of 0.1 mmHg for 100 minutes, to give a resin. The inherent viscosity of the thus obtained resin was 0.72 dl/g and the glass transition temperature and the melting point were 15°C and 149°C respectively. The results are shown in Table 3. Example 18 Example 15 was repeated except for using as an adhesive resin a poly(ester-amide) having an inherent viscosity of 0.75 dl/g comprising a copolyester modified with 41 mol% of piperazine: [poly(piperazine/1,4-cyclohexanedimethanol/azelate = 41/9/50 (molar ratio)]. The then molar ratio of ester group/amide group was 18/82. The results are shown in Table 3. Example 19 Example 15 was repeated except for using as an adhesive resin a resin obtained by blending 100 parts of a polyester having an inherent viscosity of 0.75 dl/g modified with 35 mol% of isophthalic acid: [poly(ethylene/isophthalate/terephthalate = 50/35/15 (molar ratio)] with 80 parts of 6-66 nylon, followed by pelletization using a 40-⊘ twin-screw vent-type extruder, and then by drying at 150°C for 8 hours. The then molar ratio of ester group/amide group was 60/40. The results are shown in Table 3. Example 20 Trims and rejected cups having generated during the thermoformation in Example 15 were slit, dried at 150°C for 8 hours in vacuo, and thereafter fed to a 40-⊘ vent-type extruder, followed by pelletization. The obtained pellets were dried (150°C, 8 hours in vacuo). Using the pellets, a sheet having a construction of outer PET composition layer of 500 µm thickness/recovery layer (content of the heat-resistant PET composition: 80%) of 300 µ thickness/adhesive resin layer of 50 µm thickness/PET composition layer of 50 µm thickness was obtained. The results of evaluations made in the same manner as in Example 15 are shown in Table 3. Example 21 An EVOH having a melt index (MI; 190°C, 2160 g) of 1.5 g/10 min comprising 32 mol% of ethylene, and having a saponification degree of 99.4%. As the heat-resistant crystalline PET there was used a heat-resistant polyester composition obtained by dry blending 100 parts of a polyethylene terephthalate having an inherent viscosity of 0.90 dl/g incorporating 0.1 mol% of pentaerythritol and 0.64% of benzoic acid, with 3 parts of a low density polyethylene having a MI (190°C, 2160 g) of 5.0 g/10 min, 1.2 parts of TiO₂ as a pigment and 0.5 part of Irganox 1010 (made by Ciba-Geigy) as a heat stabilizer. The composition was then pelletized at 280°C with a 40-⊘ extruder of twin-screw and vent type, followed by drying at 150°C for 8 hours. As the adhesive resin, a resin comprising a polyolefin modified with maleic anhydride (ADMER AT469C, made by Mitsui Petrochemial Co.) was used. A co-extrusion was conducted using the resins obtained above, with a 3 kind/5 layer co-extruder to obtain a sheet. The construction of the obtained sheet was PET composition (800 µm)/addhesive resin (50 µm )/EVOH (200 µm )/adhesive resin (50 µm)/PET composition (800 µm). The obtained sheet was thermoformed with a vacuum pressure forming machine equipped with a round-cup mold at the sheet temperature of 130°C and at a blowing ratio of 1. The obtained cup was heat set at the mold temperature of 180°C for 10 seconds. The obtained container had a good appearance. When the container was heated in an electric cooking oven at 220°C for 30 minutes, the shrinkage ratio (longitudinal) was 3%, the shrinkage ratio being a value calculated from the formula: 100 x (size before heating - size after heating)/size before heating . The container after the heating still showed a good appearance. The gas barrier properties of 10 pieces of the containers were determined with Type 10/50 made by Mocon Co. to give an average value of O₂ gas permeability of 0.5 cc·20 µm/m²·day·atm and a range R (maximum -minimum) of 0.15 cc·20 µm/m²·day·atm, both of which are excellent, proving that the container is highly reliable. Example 22 Example 21 was repeated except for: changing the EVOH to a modified EVOH having a MI (190°C) of 1.8 g/10 min, comprising ethylene unit in an amount of 28 mol% and having a saponification degree of 99.4%, the EVOH incorporating 0.02 mol% of vinyltrimethoxysilane, and changing the adhesive resin to a poly(ester-amide) having an inherent viscosity of 0.70 dl/g comprising azelaic acid/cyclohexane dimethanol/piperadine (molar ratio: 0.45/0.10/0.45). The obtained container was good; and when heated at 220°C for 30 minutes in an electric cooking oven, the container showed heat shrinkage of as small as 3.4% and no deformation, distortion or slackening. 10 pieces of the containers were evaluated for gas barrier property at 20°C, 65% RH, to give an average O₂ permeability of 0.1 cc·20 µm/m²·day·atm and a range R (maximum -minimum) of 0.05 cc·20 µm/m²·day·atm, both of which proving that the container is a excellent heat-resistant container. Examples 23 and 24 Details of prescriptions and results obtained are shown in Table 4. Example 25 Example 21 was repeated except for changing the linear low density polyethylene to a high density polyethylene (MI: 5.3 g/10 min). The results are shown in Table 4. Example 26 Example 21 was repeated except for changing pentaerythritol (0.1 mol%) to trimethylolpropane (0 24 mol%) and changing the linear low density polyethylene to a polypropylene (MI: 7.0 g/10 min). The results are shown in Table 4.

Claims: A heat-resistant container comprising an ethylene-vinyl alcohol copolymer layer and a polyester resin layer, characterized in that said polyester resin layer comprises a crystalline polyester resin comprising a thermoplastic polyester and a polyolefin as crystallization accelerator. The heat-resistant container according to claim 1, characterized in that the ethylene-vinyl alcohol copolymer layer contains a drying agent The heat-resistant container according to claim 1 or 2, characterized in that the thermoplastic polyester contains at least 80 mol% of ethylene terephthalate units. The heat-resistant container according to claim 2, characterized in that the ratio of said ethylene-vinyl alcohol copolymer to the drying agent is from 97 : 3 to 50 : 50 by weight. The heat-resistant container according to claim 2, characterized in that said drying agent is a salt capable of forming hydrates. The heat-resistant container according to claim 2, characterized in that said drying agent is sodium dihydrogenphosphate, sodium monohydrogen phosphate, sodium phosphate and/or sodium pyrophosphate. The heat-resistant container according to any one of claims 1 to 6, characterized in that said ethylene-vinyl alcohol is a saponified product of an ethylene-vinyl acetate copolymer having from 25 to 60 mol% of ethylene units and a saponification degree of the vinyl acetate units of at least 96%. The heat-resistant container according to any one of claims 1 to 7, characterized in that crystalline polyester layers are provided on both surfaces of said ethylene-vinyl alcohol copolymer layer. The heat-resistant container according to claim 1, characterized in that the polyolefin is a polymer obtained from olefin monomers having 2 to 6 carbon atoms, such as low density polyethylene.

Inventors: MATSUMURA KEIJI, MORITANI TOHEI, NEGI TAICHI, ODA HIDEMASA, SATO TOSHIAKI, MATSUMURA, KEIJI, MORITANI, TOHEI, NEGI, TAICHI, ODA, HIDEMASA, SATO, TOSHIAKI
Applicants: KURARAY CO, KURARAY CO., LTD.
Application year: 1988
Main classification: B65D65
IPC codes: B32B27, B65D65, B65D81