Field of the Invention This invention relates to polyester compositions that possess improved gas barrier properties. These novel polyester blends comprise repeat units of phenylenedi (oxyacetic acid). Such polyesters with improved gas barrier properties are useful in packaging applications where low gas permeability are required for protection or preservation of the contents.

Background of the Invention Phenylenedi (oxyacetic acid) can be prepared by several methods.

US 4,238,625 and US 4,935,540 describe one method of preparing phenylenedi (oxyacetic acid) through the oxidation of aryloxyethanols.

JP 3204833, JP 4091052 and JP 4173765 describe the preparation of phenylenedi (oxyacetic acid) from resorcinol and chloroacetic acid.

US 4,440,922 describes the polyester hompolymers made from phenylenedi (oxyacetic acid). However, homopolymers made from phenylenedi (oxyacetic acid) are amorphous and have low glass transition temperatures making these polyesters difficult to dry. These polyesters have low elongations and are consequently brittle. In general,

hompolymers made from phenyienedi (oxyacetic acid) are unsuitable for use as a monolayer in rigid containers.

US 4,440,922, US 4,552,948, US 4,663,426, and US 5,030,705 describe the use of copolyesters containing phenylenedi (oxyacetic acid) for containers. These copolyesters have low permeability. However, because of the high level of modification, these copolyesters are difficult to <BR> <BR> <BR> <BR> crystallize. The poor crystallization behavior of these copolyesters makes them difficult to dry and limits the amount of strain induced crystallization that occurs during container fabrication. Low levels of crystallinity in the containers often result in poorer mechanical properties and lower gas barrier.

US 5,239,045 describes copolyesters containing terephthalic acid, ethylene glycol and 0.5 to 4.5 mole % of phenylenedi (oxyacetic acid). The gas barrier properties of these copolyesters are not sufficient to meet the requirements of many container applications including beer and small soft drink containers.

US 4,959,421 describes blends of PET with copolyesters containing isophthalic acid, naphthalenedicarboxylic acid and phenylenedi (oxyacetic acid). In these gas barrier materials disclosed in the above-described specification, the barrier level is low and in order to produce a container having a sufficient gas barrier property, it is thus necessary to make the barrier layer thick. The total thickness of the container is, therefore, inconveniently increased.

The above-mentioned prior art references comprising phenylenedi (oxyacetic acid) exhibit poor crystallinity and/or gas barrier properties. The present invention overcomes the problems of poor cystallization and gas barrier properties by providing a novel polyester blend comprising pheneylenedi (oxyacetic acid) with improved gas barrier properties.

Somma of the Invention The present invention provides for polyester blend compositions, methods of making and articles of manufacture.

In one embodiment, the invention provides a polyester blend composition comprising: I. from about 5 to about 85 weight % of a polyester which is the reaction product of : (A) a repeat unit of phenylenedi (oxyacetic acid) represented by the formula (I): wherein R', R2, R3 and R4 each independently represents a hydrogen atom, an alkyl group having from 1 to 6 carbon atoms, an alkoxy group having from 1 to 6 carbon atoms, a phenyl group, a chlorine atom, a bromine atom, or a fluorine atom, or an ester derivative of phenylenedi (oxyacetic acid) of the formula I; (B) a repeat unit of a diol containing up to 24 carbon atoms; and II. from about 95 to about 15 weight % of a thermoplastic polyester of poly (ethylene terephthalate), a copolyester of poly (ethylene terephthalate) modified with from greater than 0 to about 70 mole % of a glycol comprising diethylene glycol, propanediol, butanediol, hexanediol or 1,4-

cyclohexanedimethanol, and/or a dicarboxylic acid comprising isophthalic acid or naphthalenedicarboxylic acid, or a mixture of the poly (ethylene terephthalate) copolyesters with poly (ethylene terephthalate); from about 95 to about 15 weight % of a polyester of poly (ethylene naphthalate), a poly (ethylene naphthalate) copolyester modified with from greater than 0 to about 30 mole% of a glycol comprising diethylene glycol, propanediol, butanediol, hexanediol or 1,4-cyclohexanedimethanol, and/or a dicarboxylic acid comprising isophthalic acid or terephthalic acid, or a mixture of the poly (ethylene naphthalate) copolyester with poly (ethylene naphthalate); from about 95 to about 15 weight % of poly (butylene terephthalate); from about 95 to about 15% weight of poly (trimethylene terephthalate); or from about 95 to about 15% weight of poly (butylene naphthalate).

In another embodiment the invention provides a method of producing a polyester blend comprising: blending from about 5 to about 85 weight % of a polyester I and from about 95 to about 15 weight % of polyester 11, wherein polyester I comprises: (A) a repeat unit of phenylenedi (oxyacetic acid) represented by the formula (I):

wherein R1, R2, R3 and R4 each independently represents a hydrogen atom, an alkyl group having from 1 to 6 carbon atoms, an alkoxy group having from 1 to 6 carbon atoms, a phenyl group, a chlorine atom, a bromine atom, or a fluorine atom, or an ester derivative of phenylenedi (oxyacetic acid) of the formula I; and (B) a repeat unit of a diol containing up to 24 carbon atoms; and polyester 11 comprises a thermoplastic polyester of poly (ethylene terephthalate), a copolyester of poly (ethylene terephthalate) modified with from greater than 0 to about 70 mole % of a glycol comprising diethylene glycol, propanediol, butanediol, hexanediol or 1,4- cyclohexanedimethanol, and/or a dicarboxylic acid comprising isophthalic acid or naphthalenedicarboxylic acid, or a mixture of the poly (etheylene terephthalate) copolyester with poly (ethylene terephthalate); a polyester of poly (ethylene naphthalate), a poly (ethylene naphthalate) copolyester modified with from greater than 0 to about 30 mole% of a glycol comprising diethylene glycol, propanediol, butanediol, hexanediof or 1,4-cyclohexanedimethanol, and/or a dicarboxylic acid

comprising isophthalic acid or terephthalic acid, or a mixture of the poly (ethylene naphthalate) copolyester with poly (ethylene naphthalate); a poly (butylene terephthalate); a poly (trimethylene terephthalate); or a poly (butylene naphthalate).

Additional advantages of the invention will be set forth in the description which follows, and in part will be obvious from the description, or may be leamed by practice of the invention. The advantages of the invention will be realized and attained by means of the elements and combinations particularly pointed out in the appended claims. It is to be understood that both the foregoing general description and the following detailed description are exemplary and explanantory only and are not restrictive of the invention, as claimed.

Detailed Description of the Invention The present invention may be understood more readily by reference to the following detailed description of preferred embodiments of the invention and the examples therein.

It must be noted that, as used in the specification and the appended claims, the singular forms"a,""an"and"the"include the plural referents unless the context clearly dictates otherwise.

Ranges are often expressed herein as from"about"one particular value, andlor to"about"another particular value. When such a range is expressed, another embodiment includes from the one particular value and/or to the other particular value. Similarly, when values are expressed as approximations, by use of the antecedent"about,"it will be understood that the particular value forms another embodiment.

A weight percent of a component, unless specifically stated to the contrary, is based on the total weight of the formulation or composition in which the component is included.

With respect to the polyesters, mole % are based on 100 mole % diacid and 100 mole % diol, for a total 200 mole %.

"Optional"or"optionally"means that the subsequently described event or circumstances may or may not occur, and that the description inclues instances where said event or circumstances occurs and instances where it does not. For example, the phrase"optionally substituted lower alkyl"means that the alkyl group may or may not be substituted and that the description inclues both unsubstituted lower alkyl and lower alkyl where there is substitution.

The term °adjacent"means that the layers in the multi-layered structure are in close proximity to one another, and may or may not impiy that the layers are in direct contact with one another.

The term °contact"means that the layers in the multi-layered structure are touching one another, and are not separated by an intermediate layer.

Preferred phenylenedi (oxyacetic acids) of formula C) include 1,2- phenylenedi (oxyacetic acid), 1,3-phenylenedi (oxyacetic acid), 1,4- phenylenedi (oxyacetic acid), 2-methyl-1,3-phenylenedi (oxycetic acid), 5- methyl-1,3-phenylenedi (oxyacetic acid), 4-methyl-1,3-phenylenedi (oxacetic acid), 5-ethyl-1,3-phenylenedi (oxyacetic acid), 4-ethyl-1,3 phenylenedi (oxyacetic acid), 5-methoxy-1,3 phenylenedi (oxyacetic acid), 4- methoxy-1,3 phenylenedi (oxyacetic acid), 4-chloro-1,2-phenylenedi (oxyacetic acid), or 4-chloro-1,3-pheny ! enedi (oxyacetic acid), or an ester thereof.

An even more preferred phenylenedi (oxyacetic acid) of formula (I) inclues a derivative of 1,2-phenylenedi (oxyacetic acid), 1,3-

phenylenedi (oxyacetic acid), or 1,4-phenylenedi (oxyacetic acid), or an ester thereof.

Phenylenedi (oxyacetic acids) as the dicarboxylic acid component (IA) in the present invention may be used as a raw material of a polyester of the present invention either in the form of an acid itself or in the form of an ester forming derivative such as an acid halide and an ester, in particular, an ester forming derivative such as a C1-4 alkyl phenylenedi (oxyacetic acid) ester. Alternatively, an oligomer obtained by reacting a phenylenedi (oxyacetic acid) with a glycol may be used for polymerization.

The polyester component I is present in the range of from about 5 to about 85 weight % of the blend composition, more preferably from about 5 to about 60 weight % of the blend composition, and most preferably from about 5 to about 40 weight % of the blend composition.

As the diol component (IB) for a polyester of the present invention, typical diols include ethylene glycol, 1,2-propanediol, 1,3-propanediol, 1,4- butanediol, pentamethylene glycol, hexamethylene glycol, neopentyl glycol, cyclohexanedimethanol, 1,3 bis (2-hydroxyethoxy) benzene, or diethylene glycol, or a derivative of an aromatic dihydroxy compound. A preferable diol component is ethylene glycol, and typical aromatic dihydroxy derivatives include resorcinol, hydroquinone, Bisphenol A, or Bisphenol S.

The polyester component 11 is present in the range of from about 95 to about 15 weight % of the blend composition, more preferably from about 95 to about 40 weight % of the blend composition, most preferably from about 95 to about 60 weight % of the blend composition.

A polyester blend of the present invention may contain a polyfunctional compound such as trimethylolpropane, pentacrythritol, glycerin, trimellitic acid, trimesic acid, or pyromellitic acid, or a monofunctional compound such as o-benzoylbenzoic acid in the range which does not impair the effect of the present invention.

The polyfuncfional or monofunctional compound may be added to the resultant polyester blend comprising phenylenedi (oxyacetic acid), or the polyfunctional or multifunctional compound may be employed as an additional monomeric component to form the polyester of phenlyenedi (oxyacetic acid). Such a polyfunctional or monofunctional compound is preferably used in the range of not more than 20 mol % of the diol component (IB).

The preparation of phenylenedi (oxyacetic acid) monomers is disclosed in US 4,935,540, the teachings of which are incorporated herein by reference.

The polyesters (I or 11) of the present invention preferably have an <BR> <BR> <BR> intrinsic viscosity of 0.4 to 2.0, preferably 0.50 to 1.2 [measured at 25° C by using a mixed solvent of phenol and tetrachloroethane (in a weight ratio of 60: 40)]. If the intrinsic viscosity is less than 0.4, the strength of the polyester obtained is so low that it is impossible to obtain practically necessary physical properties when the polyester is taken out of the reaction vessel after polymerization and cut into chips. On the other hand, if the intrinsic viscosity exceeds 2.0, the melting viscosity becomes so high as to make subsequent processing difficult.

The polyesters (I or 11) of the present invention can be produced by any polymerization method that is conventionally known for a polymerization method for poly (ethylene terephthalate). For example, a polycondensation method may be adopted, which comprises the steps of directly esterifying a phenylenedi (oxyacetic acid) represented by the formula [1] such as 1,3-phenylenedi (oxyacetic acid) and ethylene glycol under a pressure and thereafter gradually reducing the pressure while raising the temperature to polycondense the reaction product. It is also possible to produce a copolymerized polyester of the present invention by subjecting an ester derivative of a phenylenedi (oxyacetic acid) represented by the general formula [l] such as dimethyl 1,3-phenylenedi (oxyacetate)

and ethylene glycol to an ester exchange reaction, and further polycondensing the reaction product.

In the production of such a polymer, (I or li) it is preferable to use an esterifying catalyst, ester exchanging catalyst, polycondensation catalyst, stabilizer, etc.

As the ester exchanging catalyst, at least one known compound selected from calcium, manganese, zinc, sodium and lithium compounds is usable. From the point of view of transparency, a manganese compound is more preferable. As the polycondensation catalyst, at least one known compound selected from antimony, germanium, titanium and cobalt compounds is usable. Antimony, germanium and titanium compounds are preferably used.

The polyester blends are prepared by using conventional melt blending equipment such as Brabender extruder equipment, single-screw extruders, twin-screw extruders and the like. The blends are generally processed at temperatures in the range of about 240°C to about 330°C.

Properties of the blends may be altered significantly depending on the mixing temperature and mixing time. Generally, processing times in the range of 0.4 to about 5 minutes are useful to achieve the desired results.

Conventionally known additives include, but are not limited to an additive of an antioxidant, ultraviolet absorber, fluorescent brightener, mold release agent, antistatic agent, dispersant, reheat enhancing aid, acetaldehyde reducing additive, nanoparticle, coloring agent such as a dye or a pigment, or a mixture thereof may be added, if necessary, to a polyester blend in the present invention at any manufacturing stage.

Alternatively, such an additive may be added before molding by what is called master batching. Additives may be added in any amount and combination so long as they do not detract from the purpose (s) of the present invention.

A polyester blend of the present invention may be subjected to heat treatment, if necessary, before use so as to reduce acetaidehyde or lower the oligomerization degree. Alternatively, a polyester blend of the present invention may also be subjected to solid-state polymerization before use so as to enhance the polymerization degree, reduce acetaidehyde or lower the oligomerization degree.

The heat treatment is preferably carried out at 30° C to a temperature directly below the melting point, for several to several hundred hours. The solid-state polymerization is preferably carried out to 120° C to a temperature directly below the melting point, preferably 140° to 230° C for less than several ten hours preferably 5 to 30 hours after the surfaces of the chips are crystallized at a temperature of 80° to 200° C.

The polyester blend compositions of the present invention can be crystallized and dried prior to processing to remove moisture in order to prevent degradation during processing. The polyester blend compositions are crystallized at a temperature of 80° to 200°C. The polyester blend compositions are dried in either an inert atmosphere, dry air atmosphere or under reduced pressure at 30° to 200°C for several to several hundred hours. Preferably, the polyester blend compositions are dried at 80° to 180°C for 2 to 40 hours.

In order to produce a hollow molded product of the polyester blend of the present invention, for example, a blow molding method such as a hot parison process or a cold parison process is adopted in which a preform is first produced by ordinary extrusion blow molding, injection blow molding, injection molding or extrusion molding, and the thus obtained preform is reheated and biaxially stretched as it is or after processing the mouth portion and the bottom portion.

It is also possible to form a uniaxially or biaxially stretched film from a polyester of the present invention or a can-shaped container, a tray or the like by vacuum forming or air-pressure forming after it is formed into a sheet

by injection molding. It is also possible to form a polyester blend of the present invention into a multi-layered sheet of the polyester blend and poly (ethylene terephthalate), for example, by a multi-layer extruder and thereafter form the sheet into a uniaxially or biaxially stretched film, a can- shaped container or a tray.

A polyester blend composition of the present invention can be formed into a film, sheet, container, bottle, or other packaging material by a melt molding method which is generally used in molding poly (ethylene terephthalate). The polyester composition is usable as a material having a high gas barrier property in an unstretched state. By stretching the polyester composition at least uniaxially, it is possible to improve the gas barrier property and the mechanical strength.

A stretched sheet of a polyester blend composition of the present invention is produced by stretching a polyester blend composition of the present invention which has been formed into a sheet by injection molding or extrusion molding. The stretching method adopted may be freely selected from uniaxially stretching, sequential biaxially stretching and simultaneous biaxially stretching. It is also possible to form a stretched sheet of a polyester composition of the present invention into a cup or a tray by air-pressure forming.

When a stretched sheet of a polyester blend composition of the present invention is produced, the stretching temperature is set between the glass transition point (Tg) of the polyester and a temperature 70° C higher than the glass transition point (Tg) as in the case of producing a stretched sheet of a copolymerized polyester of the present invention. The stretching ratio is ordinarily 1.1 to 10 times, preferably 1.1 to 8 times in the case of uniaxial stretching, and 1.1 to 8 times, preferably 1.1 to 5 times in both machine and transverse directions in the case of biaxial stretching.

The thus obtained stretched sheet of a polyester blend composition of the present invention is excellent in gas barrier property and mechanical

strength and is useful as a packaging material in the form of a film, a cup or a tray.

A polyester hollow molded product of the present invention is produced by stretching and blowing the preform produced from a polyester blend composition of the present invention. It is, therefore, possible to use an apparatus conventionally used in. the blow molding of poly (ethylene terephthalate). More specifically, a blow molding method such as a hot parison process or a cold parison process is adopted in which a preform is first produced by ordinary extrusion blow molding, injection blow molding, injection molding or extrusion molding, and the thus obtained preform is reheated and biaxially stretched. The stretching temperature is 70° to 120° C, preferably 80° to 110° C, and the stretching ratio is 1.5 to 3.5 times in the machine direction and 2 to 5 times in the hoop direction.

In another embodiment, the invention provides a multi-layered structure comprising a first layer, and a barrier layer of the polyester blend composition of phenylenedi (oxyacetic acid). In this embodiment, the barrier layer is adjacent to, preferably in contact with, the first layer. The first layer may also be referred to as the main layer, inner layer, or innermost layer, and the barrier layer also referred to as the intermediate or intemal layer.

In a multi-layered structure, the first layer is typically formed from a polyester or copolyester of poly (ethylene terephthalate), and the barrier layer is formed from the polyester blend of phenylenedi (oxyacetic acid).

Additional layers in the multi-layered structure may contain the same composition as the first layer, and may be referred to as the second, third, fourth, etc. layers.

Additional barrier layers in the multi-layered structure may contain the same polyester blend phenylenedi (oxyacetic acid) as the first barrier layer, and may be referred to as the second, third, fourth, etc. barrier layers.

Further additional layers in the multi-layered structure may include an outermost layer and/or a protective layer. The outermost layer is formed

from a polyester of poly (ethylene terephthalate), or the polyester blend of phenylenedi (oxyacetic acid). The protective layer is adjacent to the outermost layer in the multi-layered structure. The protective layer may be formed from a polymer, an organic coating, or an inorganic coating, preferably polypropylene, an epoxy coating, or a silica or aluminum based coating, or the like.

When a polyester hollow molded product is produced, it is possible to first form a preform of a laminate comprising a layer of a polyester blend composition of the present invention and a layer of poly (aikylene terephthalate) mainly containing poly (ethylene terephthalate), and biaxially blow the thus obtained preform in order to produce a multi-layered hollow container. In this case, the structure of the multilayer is not restricted, but a multilayer of three to five layers is preferable.

Especially, a multi-layered structure of at least one layer of the polyester blend composition of the present invention and at least one polyester layer containing poly (ethylene terephthalate) as the main component (hereinafter referred to as the PET layer or first layer) is preferable.

The polyester of the polyester layer in the present invention may be poly (ethylene terephthalate), poly (ethylene naphthalate), poly (ethylene naphthalate) modified with from greater than 0 to about 20 mole % of terephthalic acid or polycarbonate. Preferably, the polyester of the polyester layer in the present invention is a poly (ethylene terephthalate). It is preferable that at least 80 mole % of the structural unit of the polyester is ethylene terephthalate units, and it is possible to use a dicarboxylic acid such as phthalic acid, isophthalic acid, hexahydrophthalic acid, naphthalene-dicarboxylic acid, succinic acid, adipic acid, or sebacic acid, or a polyfunctional carboxylic acid such as trimellitic acid or pyromellitic acid as an acid component in the range of from greater than 0 to about 20 mole % of the total acid component.

It is possible to use a glycol such as 1,2-propanediol, 1,3- propanediol, 1,4-butanediol, 1,6-hexanediol, neopentyl glycol, diethylene glycoi, triethylene glycol, or cyclohexanedimethanol, or a polyvalent alcohoi such as trimethylolpropane, triethylolpropane, or pentaerythritol in the range of from greater than 0 to about 40 mole % of the total alcohol component.

The intrinsic viscosity of the polyester containing poly (ethylene terephthalate) as the first layer is preferably 0.6 to 1.2 [measured at 30° C. by using a mixed solvent of phenol and tetrachloroethane (in a weight ratio of 60: 40)], and the glass transition point (Tg) thereof is preferably 70° to 80° C.

The polyester may be blended with another polyester and used as a polyester layer. In this case, the content of poly (ethylene terephthalate) in the polyester layer is preferably not less than 50%.

The polyester layer containing poly (ethylene terephthalate) as the first layer can be produced by a known polymerization method as in the polyester blend of the present invention. The polyester may be subjected to solid-state polymerization, if necessary. The solid-state polymerization is ordinarily carried out at 170° C. to a temperature directly below the melting point of the polyester, preferably 1830 to 230° C. for less than several ten hours, preferably not less than 5 hours.

A multi-layered polyester hollow container according to the present invention is produced by forming a preform of a multi-layered hollow container from a polyester blend composition and a polyester containing poly (ethylene terephthalate) as the first layer which are obtained in the above described method, and stretching the thus obtained preform at a temperature above glass transition point (Tg) of the polyester at least in the biaxial direction. The multilayer may be composed of either two layers or not less than three layers. A multilayer of three to five layers is preferable.

In this case, it is preferable that the inside layer of the hollow container is a polyester layer. The outermost layer of the hollow container may be the

polyester blend composition containing phenylenedi (oxyacetic acid), or poly (ethylene terephthalate); however, poly (ethylene terephthalate) is preferable in terms of surface strength. When the outermost layer is composed of the polyester blend composition containing phenylenedi (oxyacetic acid), a protective layer may be provided on the outside of the outermost layer for the purpose of protecting the surface.

The protective layer may be formed at a stage for forming the preform of the hollow container. Altematively, the protective layer may be formed after the preform is stretched so as to produce the hollow container by labeling or the like.

The thickness of the polyester layer and the thickness of the polyester blend layer are not specified. Generally, the total thickness of the bottle body is 200 to 700 pL, preferably 250 to 600 . The thickness of the polyester blend composition layer is different depending upon the desired barrier property, but it is generally 5 to 300 Il, preferably 10 to 200 p.

A container of the present invention is produced by extrusion blow molding or biaxial orientation blow molding which is conventionally known.

Biaxial orientation blow molding is more advantageous. In the case of using biaxial orientation blow molding, the preform of the hollow container is formed, and after the preform is heated to the stretching temperature, it is stretched within a blow mold.

In order to form a preform of the hollow container having a multi- layer structure, a bottomed preform may be formed by injection molding, or after a multi-layered pipe is formed, one end thereof may be formed into a bottom. When a preform of a hollow container having a multi-layer structure or a multi-layered pipe is produced, the layers may be formed sequentially from the innermost layer by an ordinary injection molding machine or a molding machine having a plurality of melt injection apparatuses, or the respective layers may be extruded from a plurality of injecting apparatuses into a single mold one by one, so that the

polyethylene terephthalate resin injected first may constitute the innermost layer and the outermost layer, and the phenylenedi (oxyacetic acid) polyester blend composition injected later constitutes a barrier or intermediate layer. By selecting the injection timing, it is possible to design the preform so as to have three layers, five layers or more.

The preform of the hollow container obtained is generally heated in a heating zone having a heater such as a block heater and an infrared heater for the subsequent stretching process. The heating temperature for the preform for a polyester multi-layered hollow container of the present invention is determined by the glass transition temperature (hereafter referred to as"Tg") of the polyester layer. The heating temperature is preferably in the range of Tg +5 °C to Tg +80 °C. If the heating temperature is too low, micro voids are produced due to a cold stretching and the container unfavorably presents the pearl or foggy appearance. On the other hand, if the heating temperature is too high, the preform becomes too soft to obtain a hollow container having a sufficient stretching effect.

When the preform of a polyester multi-layered hollow container is stretched to form the hollow container, the preform is preferably stretched by 1 to 4 times in the machine direction and by 2 to 6 times in the transverse direction (hoop direction of the container) by moving a rod in the machine direction and blowing pressurized air. In order to enhance the heat resistance of the container, it is possible to heat set the container by further heating the stretched hollow container within the mold at a temperature the same as or higher than the stretching temperature for a short time.

The polyester blend composition of the present invention is useful as a packaging material and can also be widely used as a container, sheet, film, bottle, etc. in the form of a blend or a laminate with other thermoplastic resins.

Particularly, a laminate of the polyester blend of the present invention with polyethylene terephthalate has a low gas permeability, so that is can be utilized very advantageously. Such a laminate can also be used together with a gas barrier material such as vinylidene chloride or a saponified ethylene-vinyl acetate copolymer.

A polyester hollow molded product of the present invention, which has a high mechanical strength as well as excellent transparency and gas barrier property, can be widely used for fresh beverage, flavoring material, oil, alcoholic drink such as beer, wine and sake, and cosmetics.

Particularly, the polyester hollow molded product of the present invention can be used as a small-sized container for carbonated drink, beer, wine or the like, which would not be preserved for a predetermined guaranteed period due to the insufficient gas barrier property by an ordinary biaxially stretched poly (ethylene terephthalate) bottle.

Especially, a polyester multi-layered hollow container of the present invention has an excellent gas barrier property, a high mechanical strength free from ply separation and an excellent transparency in the extemal appearance. A polyester multi-layered hollow container of the present invention can therefore be widely used for fresh beverage, flavoring material, oil, alcoholic drink such as beer, wine and sake, and cosmetics.

Molded articles, such as, but not limited to a bottle, sheet, fiber, film, paper, preforms, or containers formed from any of the blends disclosed above are also disclosed herein.

Examples The following examples are put forth so as to provide those of ordinary skill in the art with a complete disclosure and description of how the polyester blends claimed herein are made and evaluated, and are intended to limit the scope of what the inventors regard as their invention.

Efforts have been made to ensure accuracy with respect to the numbers (e. g. amounts, temperature, etc.) but some errors and deviations should be

accounted for. Unless indicated otherwise, parts are parts by weight, temperature is in °C or is at room temperature, and pressure is at or near atmospheric.

The present invention will be explained in more detail with reference to the following non-limitative examples.

Inherent viscosity (IhV) measurements were made at 25°C in 60/40 (w/w) phenol/tetrachloroethane solvent system.

The oxygen transmission rates of the polyester was determined in cubic centimeters permeating at 1 mil thick, 10 inches square, for a 24-hour period under an oxygen partial pressure difference of one atmosphere at 30°C using a MOCON Oxtran 100 instrument. The film actually used to measure permeability was 3-8 mils in thickness, but the permeability was converted to a one mil basis using conventional calculations. In like manner, the carbon dioxide permeability of the polyester was determined using a MOCON Permatran C instrument.

Tensile properties were measured on an Instron Universal Testing Machine. The test method used was a modified ASTM D882 for measuring the tensile properties of thin films.

Example 1 Poly (ethylene 1,4-phenylenedi (oxyacetate)) was made as follows. A reaction vessel was charged with 22.42 grams of 1,4-phenylenedi (oxyacetic acid), 24.60 grams of ethylene glycol and 100 ppm of titanium from titanium tetraisopropoxide. The reaction mixture was heated and stirred under nitrogen at 210°C for 60 minutes. The temperature was then increased to 220°C for 120 minutes until all of the water had distille out of the reaction mixture. The temperature was then raised to 260°C; the nitrogen was evacuated from the reaction system, and a vacuum was applied. The melt condensation was continued at 260°C for 75 minutes under 0.5 mm Hg pressure. The heating was discontinued, the reaction mixture was brought

to atmospheric pressure with nitrogen, and the polymer was collected. The polymer had an inherent viscosity of 0.88 dl/g.

Example 2 A melt blend of poly (ethylene terephthalate) (IhV = 0.66 dl/g) and 5 weight % of the poly (ethylene 1,4-phenylenedi (oxyacetate)) was prepared on a Brabender singie screw extruder. The blend was extruded into 5 mil and 20 mil film. The 5 mil amorphous film was characterized for IhV, Tg values, melting point, tensile properties in the machine direction and gas transmission rates. The data are listed in Table 1.

Example 3 The 20 mil film made in Example 2 was biaxially oriented 4x by 4x on a T. M. Long machine at 90°C. The oriented film was characterized for IhV, Tg values, melting point, tensile properties in the machine direction and gas transmission rates. The data are listed in Table 1.

Example 4 The same as example 2 except 10 weight % of poly (ethylene 1,4- phenylenedi (oxyacetate)) was used.

Example 5 The 20 mil film made in Example 4 was biaxially oriented 4x by 4x on a T. M. Long machine at 90°C. The oriented film was characterized for IhV, Tg values, melting point, tensile properties in the machine direction and gas transmission rates. The data are listed in Table 1.

Example 6 The same as example 2 except 20 weight % of poly (ethylene 1,4- phenylenedi (oxyacetate)) was used.

Example 7 The 20 mil film made in Example 6 was biaxially oriented 4x by 4x on a T. M. Long machine at 90°C. The oriented film was characterized for IhV, Tg values, melting point, tensile properties in the machine direction and gas transmission rates. The data are listed in Table 1.

Comparative Example 3 Poly (ethylene terephthalate) was extruded into film and characterized as described in Example 2.

Comparative Example 9 Poly (ethylene terephthalate) 20 mil film was oriented and characterized as described in Example 3.

Comparative Example 10 Poly (ethylene 1,4-phenylenedi (oxyacetate)) was extruded into film.

The IhV, Tg values, melting point, tensile properties and gas transmission rates of the amorphous film are listed in Table 1, below.

TABLE 1 Run IhV Tg Tm 02 Trans. C02 Tensl % Tensil (dl/g) (°C) (°C) Rate Trans. Stmg Elong. Mod (cc-Rate (Mpa) (Gpa) mil/100in (cc- 2-24hr-mil/100in2- atm) 24hr-atm) Ex 2 0.66 73 247 8.6 45. 8 68 386 1.83 Ex 3 0.65 78 248 5.0 19. 3 244 89 3.74 Ex 4 0.62 74 248 8.4 37. 5 56 192 2.01 Ex 5 0.63 71 246 3.9 14. 6 267 87 3.90 Ex 6 0.59 73 248 5.1 28. 2 49 323 1.88 Ex 7 0.59 71 248 2.66. 7273 83 3.84 Comp. 0.66 72 248 9.6 59. 1 46 302 1.98 Ex 8 Comp. 0.68 80 247 8.5 34.6 229 87 3.23 Ex 9 Comp. 0.63 34 nd¹ 0.7 4.5 35 5 1.93 Ex 10 nd-non detected

The present invention provides a thermoplastic polyester with reduced permeabilities to gases such as oxygen and carbon dioxide. The polyester blend compositions described in this invention have unexpectedly lower gas permeability and improved crystallization behavior.