Patent Application
20190218366
This invention relates to a formed body having excellent gas-barrier property and, more specifically, to a formed body that exhibits excellent gas-barrier property due to the use of an oxygen-absorbing component in small amounts.
Thermoplastic resins or polyester resins such as polyethylene terephthalate (PET), etc. feature such excellent properties as formability, transparency, mechanical strength, resistance against chemicals and, besides, have relatively high barrier property against gases such as oxygen and the like gases. Therefore, the polyester resins have been used in a variety of fields as packaging materials like films, sheets, and bottles. To further improve the gas-barrier property, there has been widely used an oxygen absorber.
As the oxygen absorber, there have been known inorganic oxygen absorbers such as iron powder and the like. The oxygen absorber of this kind undergoes oxidation by itself to absorb oxygen; i.e., exhibits barrier property by shutting off the permeation of oxygen. The inorganic oxygen absorber, however, causes the resin to be colored and, therefore, cannot be used in the field of packaging where transparency is required. In the field of packaging, therefore, it is a generally accepted practice to use organic oxygen absorbers that do not cause the resins to be colored.
For example, patent documents 1 to 3 filed by the present applicant are disclosing, as organic oxygen absorbers, acid anhydrides represented by the following formula;
Moreover, a patent document 4 discloses non-polymeric oxidizing organic compounds represented by the following formulas I and II;
The compounds disclosed in the above patent documents 1 to 4 exhibit oxygen-absorbing property due to their autoxidation. To gain a sufficient degree of gas-barrier property, however, these compounds had to be used in large amounts.
It is, therefore, an object of the present invention to provide a formed body that exhibits excellent gas-barrier property despite of using an oxygen-absorbing component in small amounts.
According to the present invention, there is provided a formed body of a resin having a wall portion, the wall portion containing, as an oxygen-absorbing component, a non-polymeric oxygen-absorbing organic component in an amount of 0.5 to 2.5% by mass, and having a ratio of oxygen permeation rates expressed by the following formula that is suppressed to be not more than 42%,
Ratio of oxygen permeation rates=(P/P0)×100
In the formed body of the present invention, it is desired that:
(1) The wall portion, further, contains cobalt as an oxygen-absorbing component, the content of cobalt being not more than 40 ppm; or
(2) The wall portion does not contain cobalt as the oxygen-absorbing component.
It is, further, desired that:
(3) The layer containing the oxygen-absorbing component is formed at an area ratio of 5 to 20% of the cross section of the wall portion;
(4) The formed body includes inner and outer layers of a polyester, and an intermediate layer that contains the oxygen-absorbing component, the intermediate layer being a layer in which the oxygen-absorbing component is dispersed in a matrix of a polyester;
(5) The non-polymeric oxygen-absorbing organic component is an imide compound having an unsaturated alicyclic ring in the molecules thereof; and
(6) The non-polymeric oxygen-absorbing organic component is an imide compound derived from an acid anhydride represented by the following formula (1),
Moreover, the formed body of the present invention:
(7) Has the shape of a preform for forming a container; or
(8) Has the shape of a blow-formed bottle.
The formed body of the present invention contains the oxygen-absorbing components such as non-polymeric oxygen-absorbing organic components (hereinafter often abbreviated as oxygen-absorbing organic components) that are concentrated in the wall portion thereof. By using the oxygen-absorbing organic components in only small amounts, therefore, it is made possible to suppress the ratio of the oxygen permeation rates to be not more than 42%. If reference is made to the Experimental Examples appearing later as shown in, for example,
The reason is not clear why the gas-barrier property is improved strikingly according to the present invention. The present inventors, however, presumes it as described below. First of all, the oxygen-absorbing organic components disclosed in the patent documents 1 to 4 absorb oxygen as they undergo autoxidation reaction successively through the propagation of radicals, and contribute to improving the gas-barrier property of the formed bodies. Therefore, if the oxygen-absorbing organic components are added in reduced amounts, then the distance increases among the components; i.e., radicals propagate less. Accordingly, the oxygen-absorbing organic components become no longer capable of absorbing oxygen in sufficient amounts.
In the present invention, however, the oxygen-absorbing organic components are concentrated in the center of the wall portion of the formed body such as bottle. Therefore, the distance is short among the components, and the generated radicals can be all propagated to the other oxygen-absorbing organic components. The oxygen-absorbing organic components can, therefore, be autoxidized maintaining a high degree of probability, and improved gas-barrier property is exhibited by efficiently using small amounts of the oxygen-absorbing organic components.
In addition, according to the present invention, the oxygen-absorbing organic components are made present in the center of the wall portion of a bottle or the like body in the direction of thickness effectively preventing the components from eluting out into the content. This also effectively prevents a decrease in the properties such as gas-barrier property.
Moreover, the oxygen-absorbing organic components used in the present invention are not polymers and hence can be excellently dispersed in the matrix resin making it possible to maintain transparency to a favorable degree.
The formed body of the present invention is made of a resin and contains, in the wall portion thereof, a non-polymeric oxygen-absorbing organic component as the oxygen-absorbing component.
As the resin for use in the present invention, there can be used either a thermoplastic resin or a thermosetting resin so far as it permits the non-polymeric oxygen-absorbing component that will be described later to be dispersed therein when it is formed into a formed body. From the standpoint of formability, however, it is desired to use the thermoplastic resin.
The thermoplastic resin may be a widely known one. As the widely known thermoplastic resin, there can be exemplified the following compounds.
Olefin resins such as low-density polyethylene, high-density polyethylene, polypropylene, poly 1-butene, poly 4-methyl-1-pentene, or random or block copolymers of α-olefins such as ethylene, propylene, 1-butene or 4-methyl-1-pentene, or cyclic olefin copolymers thereof;
Ethylene⋅vinyl copolymers, such as ethylene⋅vinyl acetate copolymer, ethylene⋅vinyl alcohol copolymer and ethylene⋅vinyl chloride copolymer;
Styrene resins such as polystyrene, acrylonitrile⋅styrene copolymer, ABS, and α-methylstyrene⋅styrene copolymer;
Vinyl resins such as polyvinyl chloride, polyvinylidene chloride, vinyl chloride⋅vinylidene chloride copolymer, methyl polyacrylate and methyl polymethacrylate;
Polyamide resins such as nylon 6, nylon 6-6, nylon 6/6-6 copolymer, polymetaxylileneadipamide, nylon 6-10, nylon 11, nylon 12 and nylon 13;
Polyester resins such as polyethylene terephthalate (PET), polybutylene terephthalate, polyethylene naphthalate, polytrimethylene naphthalate and copolymerized polyesters thereof;
Polycarbonate resins;
Polyphenylene oxide resins; and
Biodegradable resins such as polylactic acid;
as well as blends of these thermoplastic resins so far as they do not impair the formability.
Among the thermoplastic resins exemplified above, it is desired to use a resin that has been favorably used as a packaging material, such as olefin resin or polyester resin since it exhibits oxygen-barrier property upon absorbing oxygen and does not develop yellow color even after having absorbed oxygen. Particularly desirably, a polyester resin is used since it has a high glass transition temperature (Tg) and, therefore, can be kneaded at a high temperature so as to be formed.
The polyester resin should have a molecular weight which is at least large enough for forming a film. Preferably, therefore, there is used the polyester resin having, for example, an intrinsic viscosity (I.V.) in a range of 0.6 to 1.40 dl/g and, specifically, 0.63 to 1.30 dl/g. Specifically, there is used the one that can be biaxially stretch-blow-molded and crystallized, such as polyethylene terephthalate (PET), polybutylene terephthalate or polyethylene naphthalate. It is, further, allowable to use a blend of polyester, polycarbonate and arylate resin.
The present invention uses, particularly preferably, a PET resin of the grade of packaging in which not less than 60 mol % and, preferably, not less than 80 mol % of the ester recurring units are ethylene terephthalate units.
As the dibasic acid other than the terephthalic acid, there can be exemplified aromatic dicarboxylic acids such as isophthalic acid, phthalic acid and naphthalenedicarboxylic acid; alicyclic dicarboxylic acids such as cyclohexanedicarboxylic acid; and aliphatic dicarboxylic acids such as succinic acid, adipic acid, sebacic acid and dodecanedioic acid, which may be used in one kind or in a combination of two or more kinds. Further, as the diol component other than the ethylene glycol, there can be exemplified propylene glycol, 1,4-butane diol, diethylene glycol, 1,6-hexylene glycol, cyclohexane dimethanol and ethylene oxide adduct of bisphenol A, which may be used in one kind or in a combination of two or more kinds.
Further, the present invention favorably uses those resins that have been known as so-called gas-barrier resins. The gas-barrier resins are the resins having excellent oxygen shut-off property. Use of the gas-barrier resin as the base material resin makes it possible to lengthen the effective life of the oxygen-absorbing organic components and to exhibit excellent oxygen-barrier property over extended periods of time. It is, further, possible to improve barrier property against gases (e.g., water vapor and carbonic acid gas) in addition to oxygen.
As the gas-barrier resin, there can be exemplified nylon 6, nylon 6⋅6, nylon 6/6⋅6 copolymer, polymetaxylylenediadipamide (MXD6), nylon 6⋅10, nylon 11, nylon 12 and nylon 13. Among these polyamides, it is desired to use a polymetaxylylenediadipamide having terminal amino groups in an amount of not less than 40 eq/106 g and, specifically, not less than 50 eq/106 g since it is highly resistant against being deteriorated by oxidation.
As the gas-barrier resin other than the polyamide resin, there can be exemplified an ethylene-vinyl alcohol copolymer. For instance, there can be preferably used a saponified copolymer that is obtained by so saponifying an ethylene-vinyl acetate copolymer having an ethylene content of 20 to 60 mol % and, specifically, 25 to 50 mol % that the degree of saponification is not less than 96% and, specifically, not less than 99 mol %.
The above gas-barrier resins should have molecular weights that are at least large enough for forming films.
The present invention uses a non-polymeric oxygen-absorbing organic component as the oxygen-absorbing component.
(Non-Polymeric Oxygen-Absorbing Organic Components)
As the non-polymeric oxygen-absorbing organic component, there may be used the widely known one. As the widely known non-polymeric oxygen-absorbing component, there can be exemplified a polyene oligomer modified with an acid or an acid anhydride, such as butadiene or butadiene modified with a maleic anhydride. There can be, further, exemplified low molecular compounds having an unsaturated alicyclic ring as represented by acid anhydrides expressed by the following formula (1),
From such a standpoint that the radicals are subject to be easily generated, the oxygen-absorbing organic component is, preferably, an imide compound having an unsaturated alicyclic ring. More preferably, the oxygen-absorbing organic component is an imide compound derived from the acid anhydride expressed by the above formula (1). Specifically preferably, the oxygen-absorbing organic component is a bisimide compound that is obtained by reacting the acid anhydride expressed by the above formula (1) with a diamine. The diamine to be reacted may be an aromatic diamine. From the standpoint of avoiding the development of yellow color after having absorbed oxygen, however, an aliphatic diamine is preferred. There is no particular limitation on the aliphatic diamine provided it is capable of reacting with the above acid anhydride. The divalent aliphatic groups between the amino groups may be any of straight chain, branched chain or cyclic hydrocarbon groups. From the standpoint of highly reliably preventing the development of yellow color, however, it is desired to use an alkylenediamine which is a non-cyclic (i.e., straight chain or branched chain) alkylene group, such as methylenediamine, ethylenediamine, propylenediamine or hexamethylenediamine.
Particularly preferred oxygen-absorbing organic component is a 1,6-bis(methyltetrahydrophthalimide)hexane represented by the following formula (2),
In the present invention, the formed body contains the oxygen-absorbing organic component in an amount of 0.5 to 2.5% by mass and, preferably, 1.0 to 2.0% by mass in the wall portion thereof. If the amount of the oxygen-absorbing organic component is too small, the gas-barrier property may become unsatisfactory. If the amount of the oxygen-absorbing organic component is too large, peeling may occur in the interfaces between the region where the oxygen-absorbing organic component is concentrated and other regions.
The invention can, further, use an oxygen-absorbing assistant as the oxygen-absorbing component. For instance, there can be also used a compound having a benzylhydrogen as represented by a styrene polymer, such as polystyrene in order to further enhance the oxygen-absorbing property. The benzylhydrogen is prone to be easily pulled out, i.e., is pulled out at the time of, for example, melt-kneading, and forms a stable radical that difficulty reacts with oxygen. This could become a radical source that forms radicals of the above-mentioned oxygen-absorbing organic component and accelerates the oxidation of the oxygen-absorbing organic component upon coming in contact with oxygen. Therefore, use of the oxygen-absorbing assistant helps further improve the oxygen-absorbing capability.
In order to further improve the oxygen-absorbing capability, it is also allowable to use, as the oxygen-absorbing assistant, a transition metal catalyst that has been usually used for the formed bodies of this kind. The transition metal catalyst is added at the time of producing the base material resin or at the time of forming the body in order to absorb oxygen. As the transition metal used for the transition metal catalyst, there can be exemplified iron, cobalt, nickel, copper, silver, tin, titanium, zirconium, vanadium, chromium and manganese. However, cobalt is most desirably used from the standpoint of accelerating the oxidation of the above-mentioned oxygen-absorbing organic component and enhancing the oxygen-absorbing capability. The catalyst of the transition metal is, usually, used in the form of an inorganic salt of the transition metal of a low valence, an organic salt thereof or a complex thereof. Their concrete forms have been widely known as closely described in, for example, JP-A-2004-161796.
Use of the transition metal catalyst, however, could bring about inconveniences such as oxidation and deterioration of the resin, a resulting decrease in the strength and a decrease in the oxygen-barrier property, and could, further, by-produce low molecular decomposed products that become a cause of offensive odor. Therefore, use of the transmission metal catalyst should be limited to such a degree that the above inconveniences are negligible. Even when used, the amount thereof should be limited to be as small as possible. When the transition metal catalyst is, for example, cobalt, the amount thereof, calculated as metal, should be not more than 40 ppm and, specifically, less than 10 ppm in the wall portion of the formed body. The best way is not to use the transition metal catalyst. In the present invention, the oxygen-absorbing component is concentrated in the center in the direction of thickness. This makes it possible not only to decrease the amount of use of the oxygen-absorbing organic component as demonstrated in Examples appearing later but also to produce the oxygen-absorbing capability to a sufficient degree by using the transition metal catalyst in decreased amounts or even without using the transmission metal catalyst.
According to the present invention, further, a known N-hydroxyphthalimide compound that works as an oxidizing catalyst can be used as an oxygen-absorbing assistant in order to improve the oxygen-absorbing property. The N-hydroxyphthalimide compound permits hydrogen atoms to be easily pulled out from the N-hydroxyimide groups due to molecular oxygen, and whereby radicals are generated. The radicals then pull out the hydrogen atoms from the oxygen-absorbing organic component, and form alkyl radicals. The N-hydroxyphthalimide compound thus works as an oxidizing catalyst.
The formed body of the present invention exhibits excellent gas-barrier property despite of containing the oxygen-absorbing organic component in an amount of 2.5% by mass at the greatest. The reason why the present invention exhibits such an effect is because the wall portion contains therein a region where there are concentrated the oxygen-absorbing components, i.e., the oxygen-absorbing organic component and the oxygen-absorbing assistant that is added as required. In the bottle-like containers and preforms, the wall portion stands for a region other than the mouth portion, neck portion and bottom portion or, in other words, stands for a region from the shoulder portion to the body portion. In the cup-like and tray-like containers, the wall portion stands for a region other than the flange and the bottom portion. In the tubular containers, the wall portion stands for a region other than the mouth portion and neck portion. When the formed body of the present invention assumes the form of a film, a sheet and a bag made of them, the wall portion stands for all of them.
The formed body of the present invention may have a single-layer structure or a laminated structure so far as the oxygen-absorbing component is concentrated in the central portion in the direction of thickness. In the case of the single-layer structure, there is no interface between a region where the concentration of the oxygen-absorbing component is high and a region where the concentration of the oxygen-absorbing component is low. The region where the concentration of the oxygen-absorbing component is high may exist in a number of only one, or may exist repetitively in a plurality of numbers.
In the laminated structure, on the other hand, an interface is present between a region where the oxygen-absorbing component is dispersed and a region where there is no oxygen-absorbing component. That is, a layer where the oxygen-absorbing component is dispersed in the matrix resin (hereinafter often referred to as oxygen-absorbing layer) is provided as an intermediate layer between the inner layer and the outer layer. The laminated structure is not limited to the three-layer constitution of inner layer, outer layer and intermediate layer only but may be of a constitution of four or more layers. Further, the oxygen-absorbing layer may exist in a number of only one or may exist repetitively in a plurality of numbers.
When the formed body of the present invention has the laminated structure, it is desired that the inner layer, outer layer and intermediate layer are made of a resin of the same kind from the standpoint of close adhesion. From the standpoint of realizing a favorable oxygen-barrier property, in particular, it is further desired that the inner layer, outer layer and intermediate layer are all made of a polyester resin. Particularly preferably, from the standpoint of formability, the inner layer, outer layer and intermediate layer are all made of a PET resin, and the PET resin in the intermediate layer is lowly crystalline containing a copolymerizable component in an amount of 2 to 30 mol %. From the standpoint of separation when put to the recycling work, on the other hand, the inner layer, outer layer and intermediate layer may be made of resins of different kinds.
In the invention, the oxygen-absorbing layer may have a small thickness. From the standpoint of obtaining the effect of the invention to a maximum degree, however, it is desired that the oxygen-absorbing layer has a small thickness. Concretely speaking, the oxygen-absorbing layer is formed at an area ratio of 5 to 20% and, specifically, at an area ratio of 5 to 15% of the cross section of the wall portion. If the oxygen-absorbing layer is too thin, the gas-barrier property may not often be exhibited to a sufficient degree. Even if too thick, there is obtained no particular advantage but rather a disadvantage of an increase in the cost of production due to an increase in the amount of the oxygen-absorbing component that is used. In case there are formed a plurality of oxygen-absorbing layers, it is desired that the total thickness thereof satisfies the above numerical range.
In the invention, the thickness ratio of the sectional area of the wall portion is measured at the center in the direction of height of the wall portion of the formed body. It does not matter even if the wall portion partly includes a sectional area where there is no oxygen-absorbing component provided the amount of the oxygen-absorbing organic component, the amount of the oxygen-absorbing assistant that is added as required and the ratio of the oxygen permeation rates that will be described later, are all lying within the predetermined numerical ranges.
The position of the oxygen-absorbing layer in the direction of the thickness should be separated away from the surface of the formed body to such a degree that the oxygen-absorbing organic component is not eluted out.
The formed body of the present invention has the composition and the structure as described above. Therefore, the wall portion thereof is capable of effectively shutting off the permeation of oxygen as compared to the wall portion of a formed body that has the same thickness and that is similarly formed without, however, using the oxygen-absorbing component. Concretely speaking, the ratio of the oxygen permeation rates expressed by the following formula is suppressed to be not more than 42% and, specifically, to be 2 to 25%.
Ratio of oxygen permeation rates=(P//P0)×100
The oxygen permeation rates can be measured by a known means depending on the form of the formed body. For example, as will be described in Examples appearing later, the oxygen permeation rate can be calculated from the concentration of the dissolved oxygen that is measured by using a water dissolved oxygen concentration meter (Oxygen Indicator: manufactured by Orbisphere Laboratories, Co.).
As described above, the formed body of the present invention has not only excellent gas-barrier property but also such a property that does not permit the oxygen-absorbing component to be eluted out. Therefore, the formed body can be favorably used from a packaging material through up to a variety of applications. In the use as the packaging materials, the formed body of the invention can be used in the form of, for example, film, sheet, cup, tray, bottle or tube in order to absorb oxygen in the hermetically packed containers.
The packaging container can be formed by a means known per se., such as forming a film by the extrusion molding, and sticking the obtained films together by heat-sealing to obtain a bag-like container. It is, further, allowable to form a sheet-like or a test tube-like preform and subject the preform to the secondary forming such as vacuum forming, expansion, forming, compressed air forming, plug assist forming or blow-stretch molding to obtain a container of the form of cup, tray or bottle. Moreover, it is also allowable to directly obtain a tubular container by the extrusion molding, injection molding or direct-blow molding.
Owing to its excellent oxygen-absorbing property, the formed body of the present invention exhibits more excellent oxygen-barrier property. Therefore, the formed body, when formed as a packaging container, is very suited for containing various contents that might be deteriorated in the presence of oxygen, i.e., beverages such as beer, wine, fruit juices and carbonated soft drinks; foods such as fruits, nuts, vegetables, meat products, infant's foods, coffee, jam, mayonnaise, ketchup, edible oils, dressings, sauces, foods boiled in soy sauce, and milk products; pharmaceuticals; cosmetics; gasoline; and the like. Because of its excellent transparency, moreover, the formed body of the invention is also suited for the uses where transparency is required.
The present invention will be further described with reference to the following Experimental Examples but to which only the invention is in no way limited. Described below are the materials and the testing methods used in the following Experimental Examples.
Described below are the materials used in the Experimental Examples.
Cobalt neodecanoate (produced by OMG AMERICA, Inc.)
6 kg of a hexamethylenediamine (produced by Toray Industries Inc.) was dissolved in 57 kg of a 2-propanol in a nitrogen atmosphere, and to which was mildly added 19 kg of a mixture of the anhydrous methyltetrahydrophtalic acid (HN-2200: produced by Hitachi Chemical Co., Ltd.) that contained 45% by mass of an anhydrous 4-methyl-Δ3-tetrahydrophthalic acid and 21% by mass of an anhydrous cis-3-methyl-Δ4-tetrahydrophthalic acid such that the liquid temperature did not exceed 50° C. After thrown in whole amounts, the reaction was conducted at a temperature of 100 to 160° C. for about 7 hours while removing the generated water and the solvent to obtain a bisimide compound from the hexamethylenediamine and the anhydrous phthalic acid. As a result, there was obtained 16.7 kg of the oxygen-absorbing organic component.
By using a twin screw extruder equipped with a granulating facility (TEM-35B: manufactured by Toshiba Machine Co., Ltd.) while setting the barrel temperature at 200 to 280° C., the PET resin and the oxygen-absorbing organic component were mixed and kneaded together, and the mixture thereof was then extruded in a stranded manner to obtain a pelletized oxygen-absorbing resin. The oxygen-absorbing organic component was added in an amount of 10% by mass or 20% by mass per the total of the PET resin and the oxygen-absorbing component.
A pelletized master batch 1 was prepared by using the PET 1 as the PET resin and by using the oxygen-absorbing organic component at a concentration of 10% by mass. A pelletized master batch 2 was prepared by using the PET 1 as the PET resin and by using the oxygen-absorbing organic component at a concentration of 20% by mass. A pelletized master batch 3 was also prepared by using the PET 2 as the PET resin and by using the oxygen-absorbing organic component at a concentration of 10% by mass.
The preforms prepared in the Experimental Examples described later were cut in cross section at the center of the body portion in the direction of height. By using an optical microscope (confocal laser scan microscope manufactured by Carl Zeiss GmbH), the cross sections were observed at a magnification of 50 times. The area percentages of the oxygen-absorbing layers on the cross section of the preforms were calculated.
Since the layers in the preform have been stretched at the same ratio, the area percentages of the oxygen-absorbing layers of the bottles that are the final objects should be in substantial agreement with those of the preforms.
Oxygen-free water having an oxygen concentration of almost 0 was produced by using an oxygen-free water producing apparatus (LOW DISSOLVED OXYGEN: manufactured by Miura Industries Co., Ltd.). The bottles (full-filled capacity of 528 ml) prepared in Experimental Examples described later) were fully filled with the oxygen-free water and were sealed with a plastic cap. Next, the bottles after having been sealed were preserved in an air-conditioned chamber of 23° C.50% R.H. for 8 weeks at the longest. The concentrations of oxygen dissolved in water in the bottles after preserved were measured by using a water dissolved oxygen concentration meter (Oxygen Indicator: manufactured by Orbisphere Laboratories, Inc.).
The oxygen permeation rate (cc) was calculated from the dissolved oxygen concentration (ppm) measured in (1). Concretely, the oxygen permeation rate (cc) was calculated in compliance with the following formula by using the dissolved oxygen concentration (ppm), amount of water (528 ml) in the bottle, molar volume (24.6 L) at 23° C. and molecular weight (32.0) of oxygen.
Oxygen permeation rate (cc)=528 (ml)×dissolved oxygen concentration (ppm)×24.6 (L)×0.001/32
The oxygen permeation rate of the bottle calculated in (2) was divided by the oxygen permeation rate of the bottle (single-layered PET bottle) of Experimental Example 10 and was then multiplied by 100 to calculate the ratio of the oxygen permeation rates.
By using a co-injection molding machine, there was prepared a multilayered preform having a two-kind-three-layer (PET/intermediate layer/PET) constitution.
Concretely speaking, the PET 1 that has been dried was thrown into a hopper of the injection-molding machine for forming the inner and outer PET layers (hereinafter often abbreviated as hopper for forming the inner and outer PET layers), and the pelletized master batch 1 was thrown into a hopper of the injection-molding machine for forming the intermediate layer (hereinafter often abbreviated as hopper for forming the intermediate layer). The inner layer, outer layer and intermediate layer were all formed at a temperature of 280° C. The preform weighed 25 g. The ratio of the intermediate layer was 10% by mass of the whole preform. The preform was so molded that the intermediate layer reached neither the mouth/neck portion nor the bottom portion. The concentration of the oxygen-absorbing organic component was 1.0% by mass in the wall portion of the container.
The area ratio of the oxygen-absorbing layer was confirmed on the cross section of the obtained preform.
Next, the surface of the body portion of the multilayered preform was heated from the outer side up to 100° C. by using an infrared heater. Thereafter, the body portion was mechanically stretched in the axial direction of the bottle by using a stretch rod and, thereafter, the air was blown therein to biaxially stretch the body portion. There was thus formed a stretch-blow-molded bottle of a capacity of 500 ml, the body portion thereof being stretched by roughly 3 times longitudinally, 3 times transversely and 9 times in area. In carrying out the molding, the temperature of the mold was set at 60° C., and the high-pressure air of 3.5 MPa was blown in at room temperature (20° C.)
The obtained bottle was measured for the concentration of oxygen dissolved in water therein, and from which an oxygen permeation rate and a ratio of oxygen permeation rates were calculated.
A multilayered preform and a bottle were molded in the same manner as in Experimental Example 1 but throwing the pelletized master batch 2 to the hopper for forming the intermediate layer. The concentration of the oxygen-absorbing organic component in the wall portion of the container was 2.0% by mass. The area ratio of the oxygen-absorbing layer was confirmed on the cross section, the concentration of the dissolved oxygen was measured, the oxygen permeation rate was calculated, and the ratio of the oxygen permeation rates was also calculated.
A multilayered preform and a bottle were molded in the same manner as in Experimental Example 1 but throwing the PET 2 that has been dried into the hopper for forming the inner and outer PET layers, throwing the pelletized master batch 3 to the hopper for forming the intermediate layer, and externally adding the cobalt neodecanoate in an amount of 70 ppm calculated as metal to the pelletized master batch 3 in the hopper for forming the intermediate layer. The concentration of the oxygen-absorbing organic component in the wall portion of the container was 1.0% by mass. The concentration of cobalt in the wall portion of the container was 7 ppm. The area ratio of the oxygen-absorbing layer was confirmed on the cross section, the concentration of the dissolved oxygen was measured, the oxygen permeation rate was calculated, and the ratio of the oxygen permeation rates was also calculated.
A multilayered preform and a bottle were molded in the same manner as in Experimental Example 3 but forming the intermediate layer at a ratio of 5% by mass. The concentration of the oxygen-absorbing organic component in the wall portion of the container was 0.5% by mass. The concentration of cobalt in the wall portion of the container was 3.5 ppm. The area ratio of the oxygen-absorbing layer was confirmed on the cross section, the concentration of the dissolved oxygen was measured, the oxygen permeation rate was calculated, and the ratio of the oxygen permeation rates was also calculated.
A multilayered preform and a bottle were molded in the same manner as in Experimental Example 3 but forming the intermediate layer at a ratio of 20% by mass. The concentration of the oxygen-absorbing organic component in the wall portion of the container was 2.0% by mass. The concentration of cobalt in the wall portion of the container was 14 ppm. The area ratio of the oxygen-absorbing layer was confirmed on the cross section, the concentration of the dissolved oxygen was measured, the oxygen permeation rate was calculated, and the ratio of the oxygen permeation rates was also calculated.
A multilayered preform and a bottle were molded in the same manner as in Experimental Example 3 but blending the pelletized master batch 3 and the PET 2 at a mass ratio of 8:2, throwing the thus obtained blend into the hopper for forming the intermediate layer, and externally adding the cobalt neodecanoate in an amount of 70 ppm calculated as metal to the blend in the hopper for forming the intermediate layer. The concentration of the oxygen-absorbing organic component in the wall portion of the container was 0.8% by mass. The concentration of cobalt in the wall portion of the container was 7 ppm. The area ratio of the oxygen-absorbing layer was confirmed on the cross section, the concentration of the dissolved oxygen was measured, the oxygen permeation rate was calculated, and the ratio of the oxygen permeation rates was also calculated.
A multilayered preform and a bottle were molded in the same manner as in Experimental Example 2 but blending the pelletized master batch 3 and the PET 2 at a mass ratio of 2:8, throwing the thus obtained blend into the hopper for forming the intermediate layer, externally adding the cobalt neodecanoate in an amount of 110 ppm calculated as metal to the blend in the hopper for forming the intermediate layer, and forming the intermediate layer at a ratio of 40% by mass of the whole preform. The concentration of the oxygen-absorbing organic component in the wall portion of the container was 0.8% by mass. The concentration of cobalt in the wall portion of the container was 44 ppm. The area ratio of the oxygen-absorbing layer was confirmed on the cross section, the concentration of the dissolved oxygen was measured, the oxygen permeation rate was calculated, and the ratio of the oxygen permeation rates was also calculated.
By using a co-injection molding machine while halting the operation of the machine for injection-molding the intermediate layer, the PET 1 and the pelletized master batch 1 were blended together at a mass ratio of 9:1, and the obtained blend was thrown into the hopper of the machine for injection-molding the inner and outer PET layers. By setting the temperature at 280° C., there was molded a single-layered PET preform weighing 25 g.
Using the same method as that of Experimental Example 1, the preform was biaxially stretch-blow molded into a single-layered PET bottle. The concentration of the oxygen-absorbing organic component in the wall portion of the container was 1.0% by mass.
The concentration of the dissolved oxygen was measured, the oxygen permeation rate was calculated, and the ratio of the oxygen permeation rates was also calculated.
A single-layered bottle was molded in the same manner as in Experimental Example 8 but blending the PET 2 and pelletized master batch 3 at a mass ratio of 9:1, throwing the thus obtained blend into the hopper for forming the inner and outer PET layers, and externally adding the cobalt neodecanoate in an amount of 21 ppm calculated as metal to the blend in the hopper for forming the inner and outer PET layers. The concentration of the oxygen-absorbing organic component in the wall portion of the container was 1.0% by mass. The concentration of cobalt in the wall portion of the container was 21 ppm. The concentration of the dissolved oxygen was measured, the oxygen permeation rate was calculated, and the ratio of the oxygen permeation rates was also calculated.
A single-layered bottle was molded in the same manner as in Experimental Example 8 but throwing the PET 1 only into the hopper for forming the inner and outer PET layers. The concentration of the dissolved oxygen was measured, the oxygen permeation rate was calculated, and the ratio of the oxygen permeation rates was also calculated.
Table 1 shows the constitutions of the bottles formed by the Experimental Examples, as well as the measured and calculated results thereof. Further,
| Number | Date | Country | Kind |
|---|---|---|---|
| 2016-190039 | Sep 2016 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2017/035329 | 9/28/2017 | WO | 00 |
