Patent Application
20210229404
The present invention relates to a multilayered article and a multilayered container.
Multilayered articles and multilayered containers that use a polyester resin as a resin constituting an outer layer and an inner layer, and have a barrier layer formed from a polyamide resin between the outer layer and the inner layer have been examined in the past (Patent Documents 1 and 2).
Patent Document 1: JP 2016-169027 A
Patent Document 2: JP 60-232952 A
However, when such multilayered articles and multilayered containers having an outer layer and an inner layer formed from a polyester resin, and a barrier layer (intermediate layer) formed from a polyamide resin were examined by the present inventors, it was found that the oxygen barrier property is inferior depending on the type of polyamide resin.
The present inventors also found that when a polyamide resin (MXD6) constituted of meta-xylylenediamine and adipic acid is used as the polyamide resin, a multilayered article and a multilayered container with excellent oxygen barrier properties can be obtained. However, when a barrier layer made of MXD6 is used, the delamination resistance is not necessarily sufficient. Furthermore, when an aliphatic polyamide resin is compounded with the MXD6, the delamination resistance improves, but the oxygen barrier property may become inferior. A multilayered container of a bottle also requires transparency.
Thus, an object of the present invention is to solve the problems described above by providing a multilayered article and a multilayered container with an excellent balance between the oxygen barrier property, delamination resistance and transparency.
As a result of examinations conducted by the present inventors with focus on the abovementioned problems, the present inventors discovered that the above-mentioned problems can be solved by using, in the barrier layer, a combination of an aliphatic polyamide resin, and a polyamide resin in which 70 mol % or greater of its structural unit derived from a diamine is derived from xylylenediamine, and of its structural unit derived from a dicarboxylic acid, 30 to 65 mol % is derived from an a,w-linear aliphatic dicarboxylic acid having from 4 to 20 carbons, and from 70 to 35 mol % is derived from isophthalic acid. Specifically, the problems described above are solved by the following means <1>, and preferably by the following means <2> to <11>.
<1> A multilayered article includes a layer containing a polyester resin as a main component and a layer containing a polyamide resin as a main component, wherein
the polyamide resin included in the layer containing a polyamide resin as a main component includes from 90 to 60 parts by mass of a polyamide resin (B) per 10 to 40 parts by mass of a polyamide resin (A); the polyamide resin (A) is an aliphatic polyamide resin; and the polyamide resin (B) includes a structural unit derived from a diamine and a structural unit derived from a dicarboxylic acid, 70 mol % or greater of the structural unit derived from a diamine being derived from xylylenediamine, and of the structural unit derived from a dicarboxylic acid, from 30 to 65 mol % being derived from an α,ω-linear aliphatic dicarboxylic acid having from 4 to 20 carbons, and from 70 to 35 mol % being derived from isophthalic acid, a total of which does not exceed 100 mol %.
<2> The multilayered article according to <1>, wherein the polyamide resin (A) includes polyamide 6.
<3> The multilayered article according to <1> or <2>, wherein at least 70 mol % of the structural unit derived from a diamine in the polyamide resin (B) is derived from meta-xylylenediamine.
<4> The multilayered article according to any one of <1> to <3>, wherein from 30 to 65 mol % of the structural unit derived from a dicarboxylic acid in the polyamide resin (B) is derived from adipic acid.
<5> The multilayered article according to <1>, wherein the polyamide resin included in the layer containing a polyamide resin as a main component includes from 60 to 20 parts by mass of the polyamide resin (B) per 20 to 40 parts by mass of the polyamide resin (A); 80 mass % or more of the polyamide resin (A) is polyamide 6; 90 mol % or more of the structural unit derived from a diamine in the polyamide resin (B) is derived from meta-xylylenediamine; and of the structural unit derived from a dicarboxylic acid in the polyamide resin (B), from 30 to 65 mol % is derived from adipic acid, and from 70 to 35 mol % is derived from isophthalic acid.
<6> The multilayered article according to any one of <1> to <5>, wherein, of the structural unit derived from a dicarboxylic acid in the polyamide resin (B), from 30 to 59 mol % is derived from adipic acid, and from 70 to 41 mol % is derived from isophthalic acid.
<7> The multilayered article according to any of the <1> to <6>, wherein the polyamide resin (B) is an amorphous polyamide resin.
<8> The multilayered article according to any one of <1> to <7>, further including a layer containing a second polyester resin as a main component, the multilayered article including the layers positioned in an order of the layer containing a polyester resin as a main component, the layer containing a polyamide resin as a main component, and the layer containing a second polyester resin as a main component.
<9> The multilayered article according to any one of <1> to <8>, wherein the multilayered article is stretched.
<10> A multilayered container containing the multilayered article as in any one of <1> to <9>.
<11> The multilayered container according to <10>, wherein the container is a bottle.
According to the present invention, a multilayered article and a multilayered container comprehensively excelling in oxygen barrier properties, delamination resistance and transparency can be provided.
The contents of the present invention will be described in detail below. Note that, in the present specification, “from . . . to . . . ” is used to mean that the given numerical values are included as the lower limit value and the upper limit value, respectively.
In the present invention, the term amorphous resin means a resin that does not have a definite melting point, and more specifically, means a resin having a crystal melting enthalpy ΔHm of less than 5 J/g, preferably 3 J/g or less, and more preferably 1 J/g or less. The crystal melting enthalpy is measured in accordance with a method described in the examples below.
The multilayered article of the present invention includes a layer containing a polyester resin as a main component (hereinafter, “polyester resin layer”), and a layer containing a polyamide resin as a main component (hereinafter, “barrier layer”), the multilayered article being characterized in that the polyamide resin included in the layer containing a polyamide resin as a main component includes from 90 to 60 parts by mass of a polyamide resin (B) per 10 to 40 parts by mass of a polyamide resin (A); the polyamide resin (A) is an aliphatic polyamide resin; and the polyamide resin (B) includes a structural unit derived from a diamine and a structural unit derived from a dicarboxylic acid, 70 mol % or more of the structural unit derived from a diamine being derived from xylylenediamine, and of the structural unit derived from a dicarboxylic acid, from 30 to 65 mol % being derived from an α,ω-linear aliphatic dicarboxylic acid having from 4 to 20 carbons, and from 70 to 35 mol % being derived from isophthalic acid, a total of which does not exceed 100 mol %. Through such a configuration, a multilayered article and a multilayered container comprehensively excelling in oxygen barrier properties, delamination resistance, and transparency can be provided. Furthermore, a multilayered container also excelling in blow moldability can also be provided.
That is, a polyamide resin (MXD6) constituted from meta-xylylenediamine and adipic acid excels in an oxygen barrier property, but delamination resistance is not necessarily sufficient. On the other hand, when an aliphatic polyamide resin is blended therewith, the delamination resistance improves, but when the aliphatic polyamide resin is blended and thoroughly kneaded, the oxygen barrier property declines. In addition, transparency tends to be required in multilayered containers. In the present invention, a multilayered container that comprehensively excels in an oxygen barrier property, delamination resistance, and transparency is successfully provided by using isophthalic acid as a portion of the dicarboxylic acid components of the polyamide resin constituted from xylylenediamine and a linear aliphatic dicarboxylic acid such as adipic acid.
Furthermore, the multilayered article of the present invention can also excel in blow moldability.
The present invention will be described in detail below.
The polyester resin layer contains a polyester resin as a main component. Here, the term “main component” means that the polyester resin is the component with the largest content amount amongst components contained in the polyester resin layer. The amount of polyester resin contained in the polyester resin layer is preferably 80 mass % or more, more preferably 90 mass % or more, even more preferably 95 mass % or more, and yet even more preferably 98 mass % or more.
The inherent viscosity of the polyester resin is preferably from 0.50 to 0.90 dL/g.
One type of polyester resin may be contained alone, or two or more types of polyester resins may be contained. In a case where two or more types thereof are contained therein, the total amount is preferably within the range described above.
Polyester resins including both a first embodiment and a second embodiment described below are also given as examples of embodiments of the present invention.
The first embodiment of the polyester resin included in the polyester resin layer is a polyester resin having a melting point.
The melting point of the polyester resin in the polyester resin of the first embodiment is preferably from 100 to 300° C., more preferably from 200 to 300° C., and even more preferably from 220 to 295° C. The melting point is measured in accordance with a method described in the examples below. The same applies to the melting points below.
The polyester resin of the first embodiment has a glass transition temperature of preferably less than 90° C., more preferably 85° C. or lower, and even more preferably 80° C. or lower. The lower limit of the glass transition temperature is preferably 60° C. or higher, more preferably 65° C. or higher, and even more preferably 70° C. or higher. The use of such a polyester resin tends to provide more excellent molding processability. The glass transition temperature is measured in accordance with a method described in the examples below. The same applies to the glass transition temperatures described below.
Such a polyester resin is a polyester resin constituted by a structural unit derived from a dicarboxylic acid and a structural unit derived from a diol, in which at least 80 mol % (preferably 85 mol % or more, more preferably 90 mol % or more, and even more preferably 95 mol % or more) of the structural unit derived from a dicarboxylic acid is derived from at least one type selected from terephthalic acid and esters thereof, and at least 80 mol % (preferably 85 mol % or more, more preferably 90 mol % or more, and even more preferably 95 mol % or more) of the structural unit derived from a diol is derived from ethylene glycol. Here, the polyester resin of the first embodiment is formed from a structural unit derived from a dicarboxylic acid and a structural unit derived from a diol, but may also include a structural unit besides the structural unit derived from a dicarboxylic acid and the structural unit derived from a diol, or other moieties such as terminal groups. Typically, 95 mass % or more, and preferably 98 mass % or more of the polyester resin used in the present invention is constituted by the structural unit derived from a dicarboxylic acid and the structural unit derived from a diol. The same applies to other polyester resins.
For details on the polyester resin that can be used in the first embodiment, the disclosure of paragraphs [0064] to [0080] of JP 2016-169027 A, the contents of which are incorporated herein, can be referenced.
The second embodiment of the polyester resin included in the polyester resin layer is an amorphous polyester resin. A multilayered article with more excellent transparency is obtained by using an amorphous polyester resin.
The glass transition temperature of the amorphous polyester resin is preferably 90° C. or higher, and more preferably 100° C. or higher. The upper limit of the glass transition temperature is preferably 155° C. or lower, and more preferably 150° C. or lower. A multilayered article with more superior heat resistance is obtained by using such a polyester resin.
One example of the amorphous polyester resin is a polyester resin constituted by a structural unit derived from a dicarboxylic acid and a structural unit derived from a diol, in which at least 80 mol % (preferably at least 85 mol %, more preferably at least 90 mol %, and even more preferably at least 95 mol %) of the structural unit derived from a dicarboxylic acid is derived from at least one type selected from terephthalic acid, naphthalene dicarboxylic acid, and esters thereof, and of the structural unit derived from a diol, from 5 to 60 mol % (preferably from 15 to 60 mol %) is derived from spiroglycol and from 95 to 40 mol % (preferably from 85 to 40 mol %) is derived from ethylene glycol.
Another example of the amorphous polyester resin is a polyester resin constituted by a structural unit derived from a dicarboxylic acid and a structural unit derived from a diol, in which at least 80 mol % (preferably at least 85 mol %, more preferably at least 90 mol %, and even more preferably at least 95 mol %) of the structural unit derived from a dicarboxylic acid is derived from at least one type selected from terephthalic acid, naphthalene dicarboxylic acid, and esters thereof, and of the structural unit derived from a diol, from 90 to 10 mol % (preferably from 85 to 40 mol %) is derived from 1,4-cyclohexanedimethanol, and from 10 to 90 mol % (preferably from 15 to 60 mol %) is derived from ethylene glycol.
As the polyester resin used in the second embodiment, the polyester resins described in paragraphs [0010] to [0021] of JP 2006-111718 A, the polyester resins described in JP 2017-105873 A, and the polyester resins described in WO 2013/168804 can be referenced, and the contents of the disclosures thereof are incorporated herein.
The polyester resin layer of the present invention may contain other components within a range that does not depart from the spirit of the present invention. Specifically, various additives can be added such as antioxidants, optical stabilizers, UV absorbers, plasticizers, bulking agents, matting agents, dryness adjusting agents, antistatic agents, anti-settling agents, surfactants, flow modifiers, drying oils, waxes, colorants, reinforcing agents, surface smoothing agents, leveling agents, curing reaction accelerators, and thickening agents. For details on the other components, refer to the disclosure in paragraph [0026] of JP 2006-111718 A, the contents of which are incorporated in the present specification.
The polyamide resin contained in the layer containing a polyamide resin as a main component includes from 90 to 60 parts by mass of the polyamide resin (B) per 10 to 40 parts by mass of polyamide resin (A), preferably includes from 85 to 60 parts by mass of the polyamide resin (B) per 15 to 40 parts by mass of the polyamide resin (A), more preferably includes from 80 to 60 parts by mass of the polyamide resin (B) per 20 to 40 parts by mass of the polyamide resin (A), and even more preferably includes from 75 to 65 parts by mass of the polyamide resin (B) per 25 to 35 parts by mass of the polyamide resin (A). However, the total amount does not exceed 100 parts by mass. One of the advantages of the present invention is that, compared to a case in which MXD6 and the polyamide resin (B) are blended, when the polyamide resin (A) and the polyamide resin (B) are blended, the barrier property is not easily reduced even when the content of the polyamide resin (B) is increased.
Here, the term “main component” means that the polyamide resin is the component with the largest content amount amongst components contained in the barrier layer. The amount of the polyamide resin contained in the barrier layer is preferably 80 mass % or more, more preferably 90 mass % or more, even more preferably 95 mass % or more, and yet even more preferably 98 mass % or more.
A single type of the polyamide resin (A) and a single type of the polyamide resin (B) may be included, or two or more types of each may be included. In a case where two or more types thereof are contained therein, the total amount is preferably within the range described above.
Furthermore, when the barrier layer includes two or more types of polyamide resins (A) and/or polyamide resins (B), the polyamide resin (A) and/or the polyamide resin (B) of the largest content amount need only satisfy at least the below-described characteristics such as the glass transition temperature, and preferably, 90 mass % or more of the polyamide resin (A) and/or the polyamide resin (B) satisfies the characteristics thereof.
Note that the polyamide resin contained in the layer containing the polyamide resin as a main component may include a polyamide resin other than the polyamide resin (A) and the polyamide resin (B) at a proportion of 5 mass % or less of the total of the polyamide resin (A) and the polyamide resin (B), and preferably at a proportion from 0 to 3 mass %, and more preferably from 0 to 1 mass %.
The polyamide resin (A) used in the present invention is an aliphatic polyamide resin. Examples of the aliphatic polyamide resin include polyamide 6, polyamide 66, polyamide 10, polyamide 11, polyamide 12, polyamide 46, polyamide 610, polyamide 612, and polyamide 666. Polyamide 6, polyamide 66, and polyamide 666 are preferable, and polyamide 6 is more preferable.
The polyamide 6 referred to here is a polyamide resin having a structural unit derived from a caprolactam as a main component, but may also contain other structural units within a range that does not depart from the spirit of the present invention. Specific examples thereof include structural units derived from: the xylylenediamine described with respect to the polyamide resin (B) below, and a diamine other than xylene diamine, isophthalic acid, and α,ω-linear aliphatic dicarboxylic acids having from 4 to 20 carbons, or a dicarboxylic acid other than these. The content of these other structural units is preferably not more than 10 mass % and more preferably not more than 5 mass %, of the polyamide 6. The same applies to other aliphatic polyamide resins.
The polyamide resin (B) is constituted from a structural unit derived from a diamine and a structural unit derived from a dicarboxylic acid, and at least 70 mol % of the structural unit derived from a diamine is derived from xylylenediamine, and of the structural unit derived from a dicarboxylic acid, from 30 to 65 mol % is derived from a,co-linear aliphatic dicarboxylic acid having from 4 to 20 carbons, and from 70 to 35 mol % is derived from isophthalic acid (provided that the total does not exceed 100 mol %). By compounding such a polyamide resin, the transparency and oxygen barrier properties can be further improved. The polyamide resin (B) used in the present invention is typically an amorphous polyamide resin. By using an amorphous polyamide resin, transparency of the multilayered article can be further improved.
In the polyamide resin (B), 70 mol % or more, preferably 80 mol % or more, more preferably 90 mol % or more, even more preferably 95 mol % or more, and yet even more preferably 99 mol % or more of the structural unit derived from a diamine is derived from xylylenediamine. The xylylenediamine is preferably meta-xylylenediamine and para-xylylenediamine, and is more preferably meta-xylylenediamine.
An example of a preferred embodiment of the polyamide resin (B) of the present invention is a polyamide resin in which at least 70 mol % of the structural unit derived from a diamine is derived from meta-xylylenediamine
Examples of the diamine other than xylylenediamine include aromatic diamines such as para-phenylenediamine, and aliphatic diamines, such as 1,3-bis(aminomethyl)cyclohexane, 1,4-bis(aminomethyl)cyclohexane, tetramethylene diamine, pentamethylene diamine, hexamethylene diamine, octamethylene diamine, and nonamethylene diamine. A single type of these other diamines may be used, or two or more types thereof may be used.
In a case where a diamine other than xylylenediamine is used as the diamine component, the diamine thereof is used at a proportion of preferably 30 mol % or less, more preferably from 1 to 25 mol %, and particularly preferably from 5 to 20 mol %, of the structural unit derived from a diamine.
In the present invention, as described above, of the structural unit derived from a dicarboxylic acid in the polyamide resin (B), from 30 to 65 mol % is derived from an a,co-linear aliphatic dicarboxylic acid having from 4 to 20 carbons (preferably, an a, co-linear aliphatic dicarboxylic acid having from 4 to 8 carbons, and more preferably adipic acid), and from 70 to 35 mol % is derived from isophthalic acid.
Of the total dicarboxylic acids constituting the structural unit derived from a dicarboxylic acid in the polyamide resin (B), a lower limit of the proportion of isophthalic acid is not less than 35 mol %, preferably not less than 40 mol %, and more preferably not less than 41 mol %. The upper limit of the proportion of the isophthalic acid is not more than 70 mol %, preferably not more than 67 mol %, more preferably not more than 65 mol %, even more preferably not more than 62 mol %, and yet even more preferably not more than 60 mol %, and may be not more than 58 mol %. Setting the proportion of the isophthalic acid to such a range tends to further improve the oxygen barrier property of the multilayered article of the present invention.
Among the total dicarboxylic acids constituting the structural unit derived from a dicarboxylic acid in the polyamide resin (B), the lower limit of the ratio of α,ω-linear aliphatic dicarboxylic acid having from 4 to 20 carbons (preferably, α,ω-linear aliphatic dicarboxylic acid having from 4 to 8 carbons, and more preferably adipic acid) is not less than 30 mol %, preferably not less than 33 mol %, more preferably not less than 35 mol %, even more preferably not less than 38 mol %, and yet even more preferably not less than 40 mol %, and may even be not less than 42 mol %. The upper limit of the proportion of the α,ω-linear aliphatic dicarboxylic acid having from 4 to 20 carbons is not more than 65 mol %, preferably not more than 60 mol %, and more preferably not more than 59 mol %. Setting the proportion of the isophthalic acid to such a range tends to further improve the oxygen barrier property of the multilayered article of the present invention.
As described above, the α,ω-linear aliphatic dicarboxylic acid having from 4 to 20 carbons is preferably an α,ω-linear aliphatic dicarboxylic acid having from 4 to 8 carbons.
Examples of the α,ω-linear aliphatic dicarboxylic acid having from 4 to 20 carbons that is preferably used as the raw material dicarboxylic acid component of the polyamide resin include aliphatic dicarboxylic acids, such as succinic acid, glutaric acid, pimelic acid, suberic acid, azelaic acid, adipic acid, sebacic acid, undecanedioic acid, and dodecanedioic acid. A single type thereof can be used, or two or more types thereof can be mixed and used. Among these, adipic acid is preferable because the melting point of the polyamide resin is within an appropriate range for molding.
Among the total dicarboxylic acids constituting the structural unit derived from a dicarboxylic acid in the polyamide resin (B), the total proportion of isophthalic acid and the α,ω-linear aliphatic dicarboxylic acid having from 4 to 20 carbons is preferably not less than 90 mol %, more preferably not less than 95 mol %, and even more preferably not less than 98 mol %, and may be 100 mol %. Setting the total proportion of isophthalic acid and the α,ω-linear aliphatic dicarboxylic acid having from 4 to 20 carbons to such a proportion tends to further improve the transparency of the multilayered article of the present invention.
Examples of dicarboxylic acids besides isophthalic acid and α,ω-linear aliphatic dicarboxylic acids having from 4 to 20 carbons include phthalic acid compounds, such as terephthalic acid and orthophthalic acid; and naphthalene dicarboxylic acids such as 1,2-naphthalene dicarboxylic acid, 1,3-naphthalene dicarboxylic acid, 1,4-naphthalene dicarboxylic acid, 1,5-naphthalene dicarboxylic acid, 1,6-naphthalene dicarboxylic acid, 1,7-naphthalene dicarboxylic acid, 1,8-naphthalene dicarboxylic acid, 2,3-naphthalene dicarboxylic acid, 2,6-naphthalene dicarboxylic acid, and 2,7-naphthalene dicarboxylic acid. One type thereof can be used alone, or two or more types can be mixed and used.
The polyamide resin (B) is preferably substantially free of structural unit derived from terephthalic acid. Substantially free means 5 mol % or less, preferably 3 mol % or less, and even more preferably 1 mol % or less, of the molar amount of isophthalic acid contained in the polyamide resin (B). With such a configuration, suitable moldability is maintained, and the gas barrier property is less likely to change due to humidity.
Note that the polyamide resin (B) of the present invention is formed from a structural unit derived from a dicarboxylic acid and a structural unit derived from a diamine, but may also include a structural unit besides the structural unit derived from a dicarboxylic acid and the structural unit derived from a diamine, or other moieties such as terminal groups. Examples of other structural units include, but are not limited to, a structural unit derived from lactams, such as ε-caprolactam, valerolactam, laurolactam, and undecalactam, and aminocarboxylic acids, such as 11-aminoundecanoic acid and 12-aminododecanoic acid, and the like. Furthermore, the polyamide resin (B) used in the present invention may include trace amounts of components such as additives used for synthesis. Typically, 95 mass % or more, and preferably 98 mass % or more of the polyamide resin (B) used in the present invention is a structural unit derived from a dicarboxylic acid or a structural unit derived from a diamine.
The number average molecular weight (Mn) of the polyamide resin (B) is preferably 8000 or more, and more preferably 10000 or more. The upper limit of the number average molecular weight of the polyamide resin (B) is not particularly established, but may be, for example, not more than 50000, not more than 30000, or not more than 20000. An example of an embodiment of the present invention is an aspect in which the Mn of the polyamide resin (B) is smaller than the Mn of the polyamide resin (A). More preferably, the Mn of the polyamide resin (B) is smaller than the Mn of the polyamide resin (A) by 5000 or more, more preferably smaller by 8000 or more, and even more preferably smaller by 10000 or more. The number average molecular weight in the present invention is measured in accordance with a method described in paragraph [0016] of WO 2017/090556, the contents of which are incorporated herein.
The glass transition temperature of the polyamide resin (B) is preferably higher than 90° C. but not higher than 150° C., more preferably from 95 to 145° C., even more preferably from 101 to 140° C., and yet even more preferably from 120 to 135° C. Such a configuration tends to further improve the delamination resistance of a multilayered container.
The polyamide resin (B) used in the present invention preferably contains phosphorus atoms at a proportion from 3 to 300 ppm by mass, more preferably from 4 to 250 ppm by mass, even more preferably from 5 to 200 ppm by mass, yet even more preferably from 20 to 100 ppm by mass, and still more preferably from 20 to 50 ppm by mass.
The barrier layer of the present invention may contain additives within a range that does not impair the purpose of the present invention, including: inorganic fillers such as glass fibers and carbon fibers; plate-shaped inorganic fillers such as glass flakes, talc, kaolin, mica, montmorillonite, and organo-modified clay; impact resistance modifiers such as various elastomers; crystal nucleating agents; lubricants such as fatty acid amide-based lubricants and fatty acid amide type compounds; antioxidants such as copper compounds, organic or inorganic halogen-based compounds, hindered phenol-based compounds, hindered amine-based compounds, hydrazine-based compounds, sulfur-based compounds, and phosphorus-based compounds; coloring inhibitors; UV absorbers such as benzotriazole-based UV absorbers; additives such as mold release agents, plasticizers, colorants, and flame retardants; and compounds containing oxidation reaction accelerators, benzoquinones, anthraquinones, and naphthoquinones.
The barrier layer (barrier resin composition) in the present invention may contain an oxidation reaction accelerator. By including an oxidation reaction accelerator, the gas barrier property of the multilayered article can be further enhanced.
The oxidation reaction accelerator may be any compound that exhibits an oxidation reaction promoting effect, but from the perspective of promoting an oxidation reaction of the polyamide resin, a compound containing a transition metal element is preferable. The transition metal element is preferably at least one selected from, of the periodic table of elements, Group VIII transition metals, manganese, copper, and zinc, and from the perspective of effectively expressing an oxygen absorption capacity, the transition metal element is more preferably at least one selected from cobalt, iron, manganese, and nickel, and is even more preferably cobalt.
In addition to use of the abovementioned metal alone, an oxidation reaction accelerator that is in the form of a low-valency oxide, an inorganic acid salt, an organic acid salt, or a complex salt containing the metals described above may be used as such an oxidation reaction accelerator. Examples of the inorganic acid salt include halides such as chlorides or bromides, and carbonates, sulfates, nitrates, phosphates, and silicates. Meanwhile, examples of the organic acid salt include carboxylates, sulfonates, and phosphonates. Moreover, transition metal complexes with β-diketones or β-keto acid esters can also be used.
In particular, in the present invention, from the perspective of favorably expressing an oxygen absorbing capacity, it is preferable to use at least one type selected from carboxylates, carbonates, acetylacetonate complexes, oxides, and halides, which contain the metal atoms described above. It is more preferable to use at least one selected from octanoates, neodecanoates, naphthenates, stearates, acetates, carbonates, and acetylacetonate complexes, and use of cobalt carboxylates such as cobalt octano ate, cobalt naphthenate, cobalt acetate, and cobalt stearate is more preferable.
The oxidation reaction accelerator described above functions not only to promote an oxidation reaction of the polyamide resin, but also as a catalyst for an oxidation reaction of an organic compound having an unsaturated carbon bond or a compound having a secondary or tertiary hydrogen in the molecule. Therefore, in order to further increase oxygen absorption capacity, various compounds in addition to the above-described oxidation reaction accelerator can also be blended in the barrier layer of the present invention. Examples include polymers of unsaturated hydrocarbons such as polybutadiene or polyisoprene, or oligomers thereof, compounds having xylylenediamine as a backbone, or compounds to which a functional group is added to enhance miscibility between the compound and a polyester.
Examples of oxidation reaction accelerators include the transition metal compounds described in paragraphs [0063] to [0066] and the oxidizable organic compounds described in paragraphs [0067] to [0072] of WO 2012/090797, the contents of which are incorporated herein.
When the oxidation reaction accelerator contains a transition metal element, the content thereof in terms of the transition metal concentration in the barrier layer is preferably from 10 to 1000 ppm by mass, more preferably from 20 to 500 ppm by mass, and even more preferably from 40 to 300 ppm by mass, from the perspective of promoting the oxidation reaction of the polyamide resin and increasing the oxygen absorption capacity of a molded product.
The transition metal concentration in the multilayered article can be measured using a known method such as, for example, ICP emission spectroscopy, ICP mass spectrometry, and fluorescent X-ray analysis.
One type of oxidation reaction accelerator may be used alone, or a combination of two or more types may be used. When two or more types are used in combination, the total amount is preferably within the range described above.
A preferable embodiment of the multilayered article of the present invention is an aspect in which the barrier layer contains from 80 to 60 parts by mass of the polyamide resin (B) per 20 to 40 parts by mass of the polyamide resin (A), in which 80 mass % or more (preferably 90 mass % or more) of the polyamide resin (A) is polyamide 6, 90 mol % or more of structural unit derived from a diamine in the polyamide resin (B) is derived from meta-xylylenediamine, and of the structural unit derived from a dicarboxylic acid in the polyamide resin (B), from 30 to 65 mol % (preferably from 30 to 59 mol %, and more preferably from 40 to 59 mol %) is derived from adipic acid, and from 70 to 35 mol % (preferably from 70 to 41 mol %, and more preferably from 60 to 41 mol %) is derived from isophthalic acid.
The multilayered article of the present invention is a multilayered article having at least one layer each of a layer containing a polyester resin as a main component (polyester resin layer) and a layer containing a polyamide resin as a main component (barrier layer). The polyester resin layer and the barrier layer are normally in contact.
The number of layers constituting the multilayered article is preferably at least three layers. In the present invention, an aspect including at least two layers of the polyester resin layer and at least one barrier layer is exemplified. In a preferable embodiment of the multilayered article of the present invention, the multilayered article further includes a layer containing a second polyester resin as a main component, and the layer containing a polyester resin as a main component, the layer containing a polyamide resin as a main component, and the layer containing a second polyester resin as a main component are positioned in this order.
More specifically, the number of layers constituting the multilayered article is more preferably from 3 to 10, and even more preferably from 3 to 5.
The number of polyester resin layers in the multilayered container is preferably from 1 to 5, and more preferably from 2 to 4. The number of barrier layers in the multilayered container is preferably from 1 to 3, and more preferably one layer or two layers.
For example, the multilayered container may be made from one polyester resin layer and one barrier layer and have a polyester resin layer/barrier layer configuration (with the polyester resin layer being an inner layer) or a barrier layer/polyester resin layer configuration (with the barrier layer being an inner layer), or may be a three layer configuration of a polyester resin layer/barrier layer/polyester resin layer made from two polyester resin layers and one barrier layer, or may be a five layer configuration of a polyester resin layer/barrier layer/polyester resin layer/barrier layer/polyester resin layer.
From the perspective of obtaining more superior delamination resistance, the barrier layer is preferably arranged at the center or at an inner side, and is more preferably arranged at an inner side. The matter of the “barrier layer is arranged at the center” means that in a cross section of the multilayered article in the thickness direction, the barrier layer is present near the center in the thickness direction. The matter of the “barrier layer is arranged at an inner side” means that in a cross section of the multilayered article in the thickness direction, the barrier layer is present at a position near the inner surface side in the thickness direction. As the position of the barrier layer of the present invention, an aspect in which the intermediate layer is the barrier layer is exemplified in JP 02-229023 A, the contents of which are incorporated herein.
In addition to the polyester resin layer and the barrier layer, the multilayered container of the present invention may also include an optional layer according to the desired performance and the like.
The multilayered article of the present invention is preferably stretched. Examples of stretching include biaxial stretch blow molding that is performed when molding a container such as a bottle.
As a preferred embodiment of the stretching of the present invention, a preform (also referred to as a parison) containing a multilayered article of the present invention is biaxially stretched and blow molded. In particular, the stretching preferably includes a step of stretching using a stretch rod and high pressure air. The details of biaxial stretch blow molding will be described later.
In the present invention, a multilayered container containing the multilayered article of the present invention is exemplified. The shape of the multilayered container is not particularly limited, and may be, for example, a molded container such as a bottle, a cup, a tube, a tray, or a storage container, or may be a bag-shaped container such as a pouch, a standing pouch, or a zippered storage bag. In the present invention, the multilayered container is preferably a bottle.
Also, it is not necessary for all parts of the bottle to contain the multilayered article of the present invention, and particularly the barrier layer. For example, an aspect is exemplified in which the barrier layer is included in the body section of a bottle, but the barrier layer is not included in the vicinity of the opening (mouth plug section). However, the barrier layer is preferably present up to near the opening of the bottle because such a configuration provides even higher barrier performance.
From the perspective of content storage performance, the volume of the multilayered container of the present invention is preferably from 0.1 to 2.0 L, more preferably from 0.2 to 1.5 L, and even more preferably from 0.3 to 1.0 L. The thickness of the inner layer (polyester resin layer) of the multilayered container of the present invention is preferably not less than 0.01 mm, more preferably not less than 0.03 mm, and even more preferably not less than 0.05 mm, and preferably not more than 2.0 mm, more preferably not more than 1.5 mm, and even more preferably not more than 1.0 mm.
The thickness of the outer layer (polyester resin layer) is preferably not less than 0.01 mm, more preferably not less than 0.05 mm, and even more preferably not less than 0.05 mm, and is preferably not more than 2.0 mm, more preferably not more than 1.5 mm, and even more preferably not more than 1.0 mm.
The thickness of the barrier layer is preferably not less than 0.005 mm, more preferably not less than 0.01 mm, and even more preferably not less than 0.02 mm, and is preferably not more than 0.2 mm, more preferably not more than 0.15 mm, and even more preferably not more than 0.1 mm. When two or more barrier layers are provided, the total of the thicknesses of each barrier layer is preferably the thickness described above.
In addition, when two or more barrier layers are included and an intermediate layer is provided between a barrier layer and another barrier layer, the thickness of the intermediate layer is preferably not less than 0.01 mm, more preferably not less than 0.03 mm or more, and even more preferably not less than 0.05 mm, and is preferably not more than 2.0 mm, more preferably not more than 1.5 mm, and even more preferably not more than 1.0 mm.
The mass of the barrier layer in the multilayered container (in particular, a bottle) of the present invention is preferably from 1 to 20 mass %, more preferably from 2 to 15 mass %, and particularly preferably from 3 to 10 mass %, relative to the total mass of the multilayered container. By setting the mass of the barrier layer to within the range described above, a multilayered container exhibiting a good gas barrier property can be obtained, and molding into the multilayered container from a parison, which is a precursor of the multilayered container, is also facilitated.
The target content to be stored in the multilayered container of the present invention is not particularly limited, and examples include food products, cosmetics, pharmaceuticals, toiletries, mechanical, electrical and electronic components, oils, and resins, and the multilayered container of the present invention can be suitably used particularly as a container for storing food products.
Examples thereof include processed fishery products, processed livestock products, rice, and liquid foods. The multilayered container of the present invention is particularly suitable for storing foods that are easily affected by oxygen. For details thereof, refer to the descriptions in paragraphs [0032] to [0035] of JP 2011-37199 A, the contents of which are incorporated herein.
The food product to be filled into the multilayered container of the present invention is not particularly limited, but specific examples include beverages such as vegetable juice, fruit juice, teas, coffee and coffee beverages, milk and milk beverages, mineral water, ionic beverages, alcoholic beverages, fermented milk beverages, and soy milk; gel foods such as tofu, egg tofus, jellies, puddings, soft adzuki-bean jelly, mousse, yogurts, an apricot bean curd; seasonings such as sauces, soy sauce, ketchup, noodle soup bases, Japanese sauces, vinegar, mirin, dressings, jams, mayonnaise, miso, pickles, and grated spices, etc.; processed meat products such as salami, ham, sausage, yakitori, meatballs, hamburger, grilled pork, and beef jerky; processed fishery products such as kamaboko, shellfish, boiled fish, and tube-shaped fish paste cakes; processed rice products such as rice gruel, cooked rice, rice casserole, and red rice; sauces such as meat sauce, mabo sauce, pasta sauce, curry, stews, and hash sauce; dairy products such as cheese, butter, cream, and condensed milk; processed egg products such as boiled eggs and soft boiled eggs; boiled vegetables and boiled beans; side dishes such as fried foods, steamed foods, stir fry, boiled foods, and baked foods; Japanese pickled vegetables; noodles and pastas such as udon, soba, and spaghetti; and pickled fruit syrups.
Depending on the target content to be stored, the multilayered container may be disinfected or sterilized using ultraviolet rays, electron beams, gamma rays, X-rays, and the like.
The method for manufacturing the multilayered article of the present invention is not particularly specified, and a well-known method for manufacturing a multilayered article can be adopted.
When the multilayered article is to be manufactured, it is preferable to prepare a polyester resin composition to configure the polyester resin layer and a barrier resin composition to configure the barrier layer (hereinafter, these are collectively referred to as “resin compositions”). The barrier resin composition uses at least two types of polyamide resins including a polyamide resin (A) and polyamide resin (B), but the method for blending the polyamide resin (A) and the polyamide resin (B) is not particularly limited, and the resin compositions may be dry-blended and supplied when fabricating a preform for a bottle, or may be melt blended using a single screw extruder, a twin screw extruder, or the like prior to fabricating the preform, or a master batch may be prepared for use by melt blending a portion of the resins. The same applies to a case in which the polyester resin composition contains two or more resins.
Furthermore, when compounding an oxidation reaction accelerator in the barrier layer, the accelerator may be dry blended together with the polyamide resin, or may be formed in a master batch with a portion of the polyamide resin, and then blended, or may be melt-blended.
An appropriate method for manufacturing the multilayered article is selected with consideration of the structure and the like of the molded product containing the multilayered article.
For example, when molding a film or sheet, a resin composition that has been melted through a T die, a circular die, or the like can be extruded from an extruder to manufacture the film or sheet. The obtained film can also be stretched and processed into a stretched film.
Moreover, a bottle shaped package container can be obtained by injecting a molten resin composition into a mold from an injection molding machine to manufacture a preform, and then subjecting the preform to blow stretching (injection blow molding, injection stretch blow molding). Alternatively, a bottle shaped package container can be obtained by blowing, in a mold, a parison obtained by extruding a molten resin composition into the mold from an extruder (direct blow molding).
A container such as a tray or a cup can be molded and obtained by a method of injecting a molten resin composition into a mold from an injection molding machine, or by a molding method such as vacuum molding or pressure molding a sheet.
The multilayered container of the present invention is preferably manufactured by subjecting a preform to biaxial stretch blow molding. The multilayered container of the present invention may be cold parison molded or hot parison molded.
Cold parison molding (two-stage molding) is a molding process in which an injection molded preform is cooled to room temperature and stored, and then reheated with another device and supplied to blow molding. Hot parison molding (one stage molding) is a method of blow molding a parison by preheating at the time of injection molding and adjusting the temperature prior to blowing without completely cooling the parison to room temperature. In hot parison molding, in many cases, an injection molding machine, a temperature control zone, and a blow molding machine are provided in the same molding machine unit, and preform injection molding and blow molding are performed.
A first embodiment of the method for manufacturing a multilayered container of the present invention is an aspect of molding through cold parison molding. The first embodiment of the manufacturing method is described below in accordance with
Next, the heated preform is biaxially stretched and blow molded. Namely, the preform is placed in a mold 3 ((2) of
After blow molding, the mold 3 is removed to obtain a multilayered container 5 ((5) in
A second embodiment of the method for manufacturing a multilayered container of the present invention is an aspect of molding through hot parison molding. In hot parison molding, a parison is blow molded by preheating at the time of injection molding and adjusting the temperature prior to blowing in one stage without completely cooling the parison to room temperature, and the parison is molded without passing through the above-described step of (1) in
In cold parison molding and hot parison molding, the parison temperature before blow molding is determined with consideration of the glass transition temperatures (Tg) of the polyester resin constituting the polyester resin layer and the polyamide resin constituting the barrier layer. The matter of before blow molding refers to, for example, immediately prior to being blown after passing through a preheating zone. The parison temperature is preferably a temperature more than the glass transition temperature (Tgmax) of the resin having the highest glass transition temperature among the polyester resin and the polyamide resin constituting the multilayered article of the present invention, and a temperature range of Tgmax+0.1° C. to 50° C. is more preferable. Furthermore, a difference between the glass transition temperature (Tgmin) of the resin having the lowest glass transition temperature among the polyester resin and the polyamide resin, and the abovementioned Tgmax is preferably not more than 40° C., and more preferably not more than 30° C. When the parison temperature and glass transition temperatures are set to satisfy such ranges, blow moldability tends to further improve.
Furthermore, when the polyester resin and/or the polyamide resin is a crystalline resin, a difference between a lowest temperature (Tcmin) among the crystallization temperatures (Tc) of the crystalline resins, and the highest temperature (Tgmax) is preferably large. Specifically, Tcmin-Tgmax is preferably 5° C. or higher, and more preferably 10° C. or higher. An upper limit of 100° C. for Tcmin-Tgmax is practical. When the difference is set to such a range, blow moldability tends to further improve.
In addition, as the method for manufacturing a multilayered container of the present invention, the descriptions of paragraphs [0070]-[0074] of JP 2016-198912, paragraphs [0085] to [0119] of JP 2016-169027, and JP 60-232952 A can be referenced within a range that does not depart from the spirit of the present invention, and the contents thereof are incorporated herein.
The present invention is described in greater detail below through examples. The materials, usage amounts, proportions, processing details, processing procedures, and the like described in the examples below may be changed, as appropriate, as long as there is no deviation from the spirit of the present invention. Therefore, the scope of the present invention is not limited to the specific examples described below.
A reaction vessel equipped with a stirrer, a partial condenser, a total condenser, a thermometer, a dropping funnel, a nitrogen gas introduction tube, and a strand die was charged with weighed raw materials including 6001 g (41.06 mol) of adipic acid, 6821 g (41.06 mol) of isophthalic acid, 1.73 g of calcium hypophosphite (Ca(H2PO2)2) (30 ppm by mass as a phosphorus atom concentration in the polyamide resin), and 1.11 g of sodium acetate, and then sufficiently purged with nitrogen, after which the reaction vessel was filled with nitrogen to an internal pressure of 0.4 MPa, and the inside of the system was heated to 190° C. while stirring under a small nitrogen gas flow. The molar ratio of sodium acetate/calcium hypophosphite was 1.33.
To this, 11185 g (82.12 mol) of meta-xylylenediamine was added dropwise under stirring, and the temperature inside the system was continuously increased while removing condensed water that was produced, to outside of the system. After dropwise addition of the meta-xylylenediamine was completed, the internal temperature was increased, and when the temperature reached 265° C., the pressure inside the reaction vessel was reduced. The internal temperature was then further increased, and a melt polycondensation reaction was continued for 10 minutes at 270° C. Subsequently, the inside of the system was pressurized with nitrogen, and the obtained polymer was removed from the strand die and pelletized to obtain approximately 21 kg of polyamide resin pellets (MXD6I (IPA 50 mol %). The obtained polyamide resin (MXD6I (IPA 50 mol %)) was vacuum dried at 115° C. for 24 hours.
It was found that the polyamide resin (MXD6I (IPA 50 mol %)) had a crystal melting enthalpy ΔHm of substantially 0 J/g in the process of increasing the temperature, and was amorphous. The number average molecular weight was 13500. The Tg was 127° C.
A jacketed 50 L reactor equipped with a stirrer, a partial condenser, a cooler, a thermometer, a dripping tank, and a nitrogen gas introduction tube was charged with 15 kg of adipic acid, 13.1 g of sodium hypophosphite monohydrate, and 6.9 g of sodium acetate, and then sufficiently purged with nitrogen and heated to 180° C. under a small nitrogen gas flow to uniformly melt the adipic acid, after which 13.9 kg of meta-xylylenediamine was added dropwise over 170 minutes while the system was stirred. During this time, the internal temperature was continuously increased to 245° C. Note that the water produced by polycondensation was removed from the system through the partial condenser and the cooler. After the completion of dropwise addition of the meta-xylylenediamine, the internal temperature was further increased to 260° C., and the reaction was continued for 1 hour, after which a polymer was removed as a strand from a nozzle at the bottom of the reactor, and cooled with water and then pelletized to obtain a pelletized polymer.
Next, the polymer obtained through the above operation was inserted into a 50 L rotary tumbler equipped with a heating jacket, a nitrogen gas introduction tube, and a vacuum line, and the pressure in the system was reduced while rotating the tumbler, after which the pressure was returned to normal pressure using nitrogen of a purity of 99 vol. % or more. This operation was performed three times. Subsequently, the temperature inside the system was increased to 140° C. under nitrogen circulation. Next, the pressure inside the system was reduced, the temperature in the system was continuously increased to 190° C. and held for 30 minutes at 190° C., after which nitrogen was introduced to return the inside of the system to normal pressure, and then the reaction system was cooled to obtain a polyamide resin (MXD6).
The melting point of the obtained polyamide resin was 237° C., the number average molecular weight was 26000, and the glass transition temperature was 85° C.
A reaction vessel equipped with a stirrer, a partial condenser, a total condenser, a thermometer, a dropping funnel, a nitrogen introduction tube, and a strand die was charged with weighed raw materials including 10201 g (69.80 mol) of adipic acid, 2047 g (12.32 mol) of isophthalic acid, 1.73 g of calcium hypophosphite (Ca(H2PO2)2) (30 ppm by mass as a phosphorus atom concentration in the polyamide resin), and 1.11 g of sodium acetate, and then sufficiently purged with nitrogen, after which the reaction vessel was filled with nitrogen to an internal pressure of 0.4 MPa, and the inside of the system was heated to 190° C. while stirring under a small nitrogen gas flow. The molar ratio of sodium acetate/calcium hypophosphite was 1.33.
To this, 11185 g (82.12 mol) of meta-xylylenediamine was added dropwise under stirring, and the temperature inside the system was continuously increased while removing condensed water that was produced, to outside of the system. After dropwise addition of the meta-xylylenediamine was completed, the internal temperature was increased, and when the temperature reached 265° C., the pressure inside the reaction vessel was reduced. The internal temperature was then further increased, and a melt polycondensation reaction was continued for 10 minutes at 270° C. Subsequently, the inside of the system was pressurized with nitrogen, and the obtained polymer was removed from the strand die and pelletized to obtain approximately 20 kg of polyamide resin pellets (MXD6I (IPA 15 mol %)). The obtained polyamide resin (MXD6I (IPA 15 mol %)) was vacuum dried at 90° C. for 24 hours.
It was found that the obtained polyamide resin (MXD6I (IPA 15 mol %)) had a crystal melting enthalpy ΔHm of substantially 0 J/g in the process of increasing the temperature, and was amorphous (hardly crystalline). The number average molecular weight was 13000. The glass transition temperature Tg was 101° C.
PA6: UBE Nylon 1022B, Available from Ube Industries, Ltd.
PET-1: Unipet BK2180, available from Mitsubishi Chemical Corporation, melting point of 248° C., glass transition temperature of 75° C., and inherent viscosity=0.83 dL/g. At the time of use, a material that had been dried in a dehumidifying dryer at 150° C. for 8 hours was used. The inherent viscosity was measured using an Ubbelohde-type viscometer with the polyester resin dissolved in a mixed solvent of phenol/1,1,2,2-tetrachloroethane=6/4 (mass ratio) and maintained at 25° C.
Oxidation reaction accelerator: cobalt (II) stearate, available from Kanto Chemical Co., Inc.
Differential scanning calorimetry measurements were carried out in accordance with JIS K7121 and K7122 using a differential scanning calorimeter. A differential scanning calorimeter was used to perform measurements. The resin pellets were crushed and placed into a measurement pan of the differential scanning calorimeter, and then pretreated by increasing the temperature to 300° C. at a temperature increase rate of 10° C./min under a nitrogen atmosphere, followed by rapid cooling, after which the measurements were performed. As the measurement conditions, the temperature was increased to 300° C. at a temperature increase rate of 10° C./min, and then maintained at 300° C. for 5 minutes, after which the temperature was reduced to 100° C. at a temperature decrease rate of −5° C./min, and measurements were then carried out to determine the glass transition temperature (Tg), the melting point (Tm), and the crystal melting enthalpy (ΔHm).
As the differential scanning calorimeter, the “DSC-60” available from Shimadzu Corporation was used.
An injection molding machine having two injection cylinders, and a two-piece multilayered hot runner mold were used to produce a preform partially having a three-layer structure of (Y)/(X)/(Y) under the conditions indicated below. First, as the material constituting the layer (Y), a polyester resin (PET-1) was injected from one of the injection cylinders, and while the injection state of the layer (Y) was maintained, a resin mixture obtained by dry blending the various polyamide resins shown in Table 1, and also cobalt (II) stearate (available from Kanto Chemical Co., Inc.) as an oxidation reaction accelerator in Example 2, was injected as the material constituting the layer (X) that becomes the barrier layer, from the other injection cylinder simultaneously with the polyester resin (resin described in Table 1) constituting the layer (Y). Lastly, a necessary amount of the polyester resin (resin described in Table 1) constituting the layer (Y) was injected to fill the cavity, and thereby a preform partially having a three-layer structure of (Y)/(X)/(Y) was obtained. After the temperature of the obtained preform was adjusted to a predetermined temperature, the preform was transferred to a blow mold, and blow molding was performed as a secondary process to manufacture a bottle (volume: 500 mL). An injection blowing-integrated molding machine that included a preform injection molding zone having an injection cylinder and an injection mold, and a blow molding zone having a temperature adjustment unit and a blow mold was used.
Multilayered Container Molding Conditions
Skin-side injection cylinder temperature: 270° C.
Core-side injection cylinder temperature: 270° C.
Resin flow path temperature in mold: 275° C.
Injection mold cooling water temperature: 50° C.
Parison temperature before blowing: 140° C.
Blow mold cooling water temperature: 35° C.
Cycle time: 26 s
The blow moldability of the obtained bottles was evaluated visually as follows.
A: Cloudiness was not observed in any part of the entire bottle, and the bottle exhibited excellent transparency and permeability.
B: Slight cloudiness was observed in a portion of the bottle, but a good product was obtained by changing the heating temperature.
C: Slight cloudiness was observed throughout the entire bottle, and a good product was not obtained even by changing the heating temperature.
D: Significant cloudiness was observed in a portion of the bottle, and slight cloudiness was observed in all other portions of the bottle.
E: Bursting was observed with significant cloudiness in the entire bottle.
An oxygen permeability measuring device (product name “OX-TRAN 2/61”, available from MOCON Inc.) was used.
The bottles produced in the Examples and Comparative Examples were each filled with 100 mL of water, and under conditions of an oxygen partial pressure of 0.21 atm, a bottle internal humidity of 100% RH (relative humidity), an external humidity of 50% RH, and a temperature of 23° C., nitrogen at 1 atm was circulated inside the bottle at 20 mL/min, and the amount of oxygen included in the nitrogen after circulating inside the bottle for 200 hours was detected using a coulometric sensor, and thereby the oxygen permeability was measured.
S: 0.008 cc/(bottle·day·0.21 atm) or less
A: More than 0.008 cc/(bottle·day·0.21 atm) and less than or equal to 0.015 cc/(bottle·day·0.21 atm)
B: More than 0.015 cc/(bottle·day·0.21 atm) and less than or equal to 0.020 cc/(bottle·day·0.21 atm)
C: More than 0.020 cc/(bottle·day·0.21 atm) and less than or equal to 0.040 cc/(bottle·day·0.21 atm)
D: More than 0.040 cc/(bottle·day·0.21 atm)
The delamination resistance of each of the obtained multilayered bottles was evaluated as follows.
First, each of the bottles obtained as described above was filled with 500 mL of colored carbonated water (4.2 gas volume), and capped, after which the bottles were allowed to sit for 48 hours at 23° C. Next, the bottles were then dropped horizontally from a height of 1 m so that the body section came into contact with the floor. The delaminated locations became cloudy and could be visually distinguished, and therefore the presence or absence of delamination of the bottles was determined visually. Note that every bottle for which delamination occurred even partially was identified as a delaminated bottle. The number of test bottles was five, and a value obtained by averaging the number of drop times until delamination occurred was used.
A: The number of drop times was 100 or more.
B: The number of drop times was from 50 to 99.
C: The number of drop times was from 20 to 49.
D: The number of drop times was 19 or fewer.
The obtained 3-layer bottles were visually observed, and the appearance was evaluated as follows.
A: Cloudiness was not observed in any part of the entire bottle, and the bottle exhibited excellent transparency and permeability.
B: Slight cloudiness was observed throughout the entire bottle.
C: Significant cloudiness was observed throughout the entire bottle.
An injection molding machine (model SE130DU-CI, available from Sumitomo Heavy Industries, Ltd.) with two injection cylinders, and a two-piece multilayered hot runner mold (available from Kortec, Inc.) were used to produce a preform partially having a three-layer structure of (Y)/(X)/(Y) under the conditions indicated below.
Specifically, first, as the material constituting the layer (Y), a polyester resin (PET-1) shown in Table 1 was injected from one of the injection cylinders, and while the injection state of the layer (Y) was maintained, a resin mixture obtained by dry blending the polyamide resin (A) and the polyester resin (B) was injected as the material constituting the layer (X) that becomes the barrier layer, from the other injection cylinder along with the polyester resin (resin described in Table 1) constituting the layer (Y). Lastly, a necessary amount of the polyester resin (resin described in Table 1) constituting the layer (Y) was injected to fill the cavity, and thereby a preform (25 g) partially having a three-layer structure of (Y)/(X)/(Y) was obtained (preform indicated by reference numeral 1 in
Skin-side injection cylinder temperature: 285° C.
Core-side injection cylinder temperature: 265° C.
Resin flow path temperature in mold: 290° C.
Mold cooling water temperature: 15° C.
Cycle time: 33 s
Proportion of resin mixture constituting the barrier layer in the preform: 5 mass %
Petaloid-type bottles were obtained by biaxially stretching and blow molding the obtained preforms using a twin screw stretch blow molding device (model EFB1000ET, available from Frontier Inc.). The overall length of each bottle was 223 mm, the outer diameter was 65 mm, and the internal volume was 500 mL (surface area: 0.04 m2, body section average thickness: 0.33 mm), and the bottom part was petaloid shaped. No dimples were provided in the body section. The biaxial stretch blow molding conditions were as indicated below. The proportion of the layer (X) with respect to the total mass of the obtained bottle was 5 mass %.
Preform heating temperature:110° C.
Primary blow pressure:0.9 MPa
Secondary blow pressure:2.5 MPa
Primary blow delay time:0.30 sec
Primary blow time:0.30 sec
Secondary blow time:2.0 sec
Blow exhaust time:0.6 sec
Mold temperature:30° C.
The blow moldability, oxygen barrier properties, delamination resistance, and bottle appearance were evaluated for the obtained bottles in the same manner as in Example 1.
The results are shown in Table 1.
As is clear from the above results, the bottles of the present invention excelled in oxygen barrier properties, delamination resistance, and transparency (Examples 1 to 5). The bottles of the present invention also excelled in blow moldability.
In contrast, when the isophthalic acid ratio of MXD6I was low (Comparative Example 1), transparency was inferior. Furthermore, when the blending ratio of the aliphatic polyamide resin was large (Comparative Example 2), transparency was inferior. Furthermore, when MXD6 was used instead of MXD6I (Comparative Example 3), transparency was inferior.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2018-082858 | Apr 2018 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2019/017037 | 4/22/2019 | WO | 00 |
