JP7006738B2 - Multi-layer container, its manufacturing method, and recycled polyester manufacturing method - Google Patents

Description

The present invention relates to a multilayer container, a method for producing the same, and a method for producing recycled polyester.

The aromatic polyester resin obtained by using an aromatic dicarboxylic acid compound and an aliphatic diol compound as a monomer has transparency, mechanical performance, melt stability, solvent resistance, fragrance retention, gas barrier property, recyclability, etc. It has the feature of being excellent in. Therefore, aromatic polyester resins such as polyethylene terephthalate (PET) are widely used in various packaging materials such as films, sheets, and hollow containers. Although the polyester resin has a high gas barrier property, it is not always sufficient for applications that require a gas barrier property against further oxygen, carbon dioxide, and the like. Therefore, as a means for improving the gas barrier property of the polyester resin, aluminum oxide or silicon oxide may be vapor-deposited on a molded body or packaging container made of polyester resin, or a resin having high gas barrier performance may be deposited on a molded body or packaging container made of polyester resin. Is coated, laminated, or melt-mixed.

Examples of the gas barrier resin include polyamide resins such as nylon 6 and nylon 66, and ethylene-vinyl alcohol copolymers. Among the polyamide resins, polyxylylenedipamide obtained by polymerizing a diamine component containing xylylenediamine as a main component and a dicarboxylic acid component containing adipic acid as a main component is particularly excellent in gas barrier properties. Polyxylylene adipamide has a high gas barrier property and is laminated on a polyester resin because its glass transition temperature, melting point, and crystallinity are similar to those of polyethylene terephthalate, which is a widely used polyester resin. Easy to melt and mix. From this, polyxylylene adipamide is very suitable as a material for improving the gas barrier property of the polyester resin.

However, in the polyester resin composition containing polyamide, yellowing due to thermal history is more likely to proceed than that of polyester alone. Therefore, yellowing occurs especially in the recycling process of collecting the container and reusing the resin. Since this is a factor that lowers the commercial value of packaging containers, studies are being conducted to suppress yellowing. For example, Patent Document 1 describes a multilayer container having a polyester resin composition layer containing a polyester resin and an amino group-containing compound having an ability to suppress yellowing, a polyamide resin layer containing a polyamide resin, and a method for producing recycled polyester. It has been disclosed.

International Publication No. 2017/057463

Yellowing of recycled polyester is greatly affected by oxidation, and it is difficult to improve the oxygen barrier property of the container because yellowing is exacerbated when a material that absorbs oxygen is used in the container. There has been a demand for a container that can achieve both sex.
Therefore, the present invention provides a multi-layer container having excellent oxygen barrier properties, a multi-layer container capable of suppressing yellowing of recycled polyester during recycling, and a method for producing recycled polyester in which yellowing is suppressed. The task is to do.

As a result of diligent studies in view of the above problems, the present inventors have found that a multilayer container having a polyester layer and a polyamide layer containing a polyamide resin, a specific yellowing inhibitor, and an oxidation accelerator can solve the above problems. And came to complete the present invention.
The present invention provides the following [1] to [25].

[1] It has a polyester layer containing a polyester resin (X) and a polyamide layer containing a polyamide resin (Y), a yellowing inhibitor (A) and an oxidation accelerator (B), and contains the polyamide resin (Y). The amount is 0.05 to 7.0% by mass with respect to the total amount of the total polyamide layer and the total polyester layer, the yellowing inhibitor (A) is a dye, and the yellowing inhibitor (A) is contained. A multi-layer container in which the amount is 1 to 30 ppm with respect to the total amount of all polyamide layers and all polyester layers.
[2] The polyester resin (X) is derived from a constituent unit derived from a dicarboxylic acid containing 80 mol% or more of a constituent unit derived from terephthalic acid and a diol containing 80 mol% or more of a constituent unit derived from ethylene glycol. The multilayer container according to the above [1], which has a structural unit to be formed.
[3] The polyamide resin (Y) comprises a diamine-derived structural unit containing 80 mol% or more of a structural unit derived from xylylenediamine and a dicarboxylic acid containing 80 mol% or more of an adipic acid-derived structural unit. The multilayer container according to the above [1] or [2], which has a constituent unit from which it is derived.
[4] The multilayer container according to any one of [1] to [3] above, wherein the oxidation accelerator (B) is a compound containing a transition metal.
[5] The multilayer container according to the above [4], wherein the transition metal is at least one selected from the group consisting of cobalt, iron, manganese, and nickel.
[6] The multilayer container according to any one of [1] to [5] above, wherein the yellowing inhibitor (A) is an anthraquinone dye.
[7] The multilayer container according to any one of [1] to [6], wherein the polyamide layer further contains a greening inhibitor (C).
[8] The multilayer container according to the above [7], wherein the greening inhibitor (C) is at least one selected from the group consisting of anthraquinone dyes and azo dyes.
[9] The multilayer container according to any one of [1] to [8], wherein the polyamide layer further contains a polyester resin (Z).
[10] The multilayer container according to the above [9], wherein the content of the polyester resin (Z) in the polyamide layer is 5 to 70% by mass.
[11] The multi-layer container according to any one of [1] to [10] above, wherein the multi-layer container is a multi-layer hollow container.
[12] The multi-layer container according to any one of the above [1] to [11], wherein the multi-layer container has a 2- to 5-layer structure and the outermost layer is a polyester layer.
[13] The multi-layer container according to any one of the above [1] to [12], wherein the multi-layer container has a 3 to 5 layer structure, and the outermost layer and the innermost layer are polyester layers.
[14] It has a polyester layer containing a polyester resin (X) and a polyamide layer containing a polyamide resin (Y), a yellowing inhibitor (A) and an oxidation accelerator (B), and contains the polyamide resin (Y). The amount is 0.05 to 7.0% by mass with respect to the total amount of all polyamide layers and all polyester layers, the yellowing inhibitor (A) is a dye, and the yellowing inhibitor (A) is contained. A method for producing a multilayer container in which the amount is 1 to 30 ppm with respect to the total amount of the total polyamide layer and the total polyester layer, wherein the polyamide resin (Y), the yellowing inhibitor (A), and the oxidation accelerator (B) are used. ) To prepare a polyamide resin mixture, a step 2 in which the polyamide resin mixture and a polyester resin composition containing a polyester resin (X) are co-injection molded to obtain a multilayer preform, and the multilayer. A method for manufacturing a multi-layer container, which comprises step 3 of blow-molding a preform.
[15] The method for producing a multilayer container according to the above [14], wherein the greening inhibitor (C) is further mixed in step 1.
[16] The method for producing a multilayer container according to the above [14] or [15], wherein the polyester resin (Z) is further mixed in step 1.
[17] In step 1, the polyamide resin or polyester resin, the yellowing inhibitor (A) and the oxidation accelerator (B) are kneaded and then mixed with the polyamide resin (Y). The method for manufacturing a multilayer container according to any one of them.
[18] The method for producing a multilayer container according to any one of [14] to [17] above, wherein the oxidation accelerator (B) is a compound containing a transition metal.
[19] The method for producing a multilayer container according to the above [18], wherein the transition metal is at least one selected from the group consisting of cobalt, iron, manganese, and nickel.
[20] The method for producing a multilayer container according to any one of [14] to [19] above, wherein the yellowing inhibitor (A) is an anthraquinone dye.
[21] The multilayer container according to any one of [15] to [20] above, wherein the greening inhibitor (C) is at least one selected from the group consisting of anthraquinone dyes and azo dyes. Production method.
[22] A method for producing recycled polyester, which comprises a step of recovering polyester from the multilayer container according to any one of [1] to [13].
[23] The method for producing a recycled polyester according to the above [22], which comprises a step of removing all or a part of the polyamide layer from the multilayer container and recovering the polyester.
[24] The method for producing a recycled polyester according to the above [22] or [23], wherein the polyamide layer is removed by pulverizing the multilayer container and then performing wind selection separation.
[25] The production of the regenerated polyester according to any one of [22] to [24] above, wherein one or more steps selected from a crystallization step and a solid phase polymerization step are carried out after the step of recovering the polyester. Method.

According to the present invention, there is provided a multi-layer container having excellent oxygen barrier properties, a multi-layer container capable of suppressing yellowing of recycled polyester during recycling, and a method for producing recycled polyester in which yellowing is suppressed. can do.

[Multi-layer container]
The multilayer container of the present invention has a polyester layer containing a polyester resin (X) and a polyamide layer containing a polyamide resin (Y), a yellowing inhibitor (A) and an oxidation accelerator (B), and is a polyamide resin ( The content of Y) is 0.05 to 7.0% by mass with respect to the total amount of the total polyamide layer and the total polyester layer, the yellowing inhibitor (A) is a dye, and the yellowing inhibitor (Y). The content of A) is 1 to 30 ppm with respect to the total amount of all the polyamide layers and all polyester layers.
The reason why the multi-layer container of the present invention can achieve both oxygen barrier properties and suppression of yellowing of recycled polyester is not clear, but it is considered as follows.
Since the oxygen barrier layer is formed by the polyamide resin and the oxidation accelerator contributes to oxygen absorption, the oxygen barrier property can be enhanced, the dye has a stable structure, and a small amount of the yellowing inhibitor is the dye. It is considered that both of these can be achieved because the yellowing of the regenerated polyester is efficiently suppressed without inhibiting the oxidation promoting action.
The "total amount of all polyamide layers and all polyester layers" is the total mass of all the polyamide layers and all polyester layers constituting the multilayer container, and if there are a plurality of layers, all of them. Is the total amount of.

<Polyester layer>
The polyester layer contains a polyester resin (X).

(Polyester resin (X))
The polyester resin (X) contained in the polyester layer is preferably a polycondensed polymer of a dicarboxylic acid and a diol, and has a structural unit derived from the dicarboxylic acid (dicarboxylic acid unit) and a structural unit derived from the diol (diol unit). Is preferable.

Examples of the dicarboxylic acid unit include a structural unit derived from an aromatic dicarboxylic acid, a structural unit derived from an alicyclic dicarboxylic acid, and a structural unit derived from an aliphatic dicarboxylic acid. preferable.
Examples of the aromatic dicarboxylic acid include terephthalic acid, isophthalic acid, orthophthalic acid, biphenyldicarboxylic acid, diphenylether-dicarboxylic acid, diphenylsulfone-dicarboxylic acid, diphenylketone-dicarboxylic acid, 2,6-naphthalenedicarboxylic acid, and 1,4-naphthalene. Examples thereof include dicarboxylic acid and 2,7-naphthalenedicarboxylic acid, and terephthalic acid, isophthalic acid, orthophthalic acid, naphthalenedicarboxylic acid, and 4,4'-biphenyldicarboxylic acid are preferable from the viewpoint of cost and ease of production. Telephthalic acid, isophthalic acid, and naphthalenedicarboxylic acid are more preferable, terephthalic acid and isophthalic acid are further preferable, and terephthalic acid is further preferable from the viewpoint of moldability.
As the aromatic dicarboxylic acid, an alkyl ester having 1 to 4 carbon atoms of the aromatic dicarboxylic acid may be used.
When the multi-layer container of the present invention is recycled, it may be melt-kneaded with a single-layer container made of a conventional polyester resin. By having a unit derived from terephthalic acid as the dicarboxylic acid unit, the compatibility between the multi-layer container of the present invention and the conventional single-layer container becomes good, and good recyclability can be obtained.

As the aromatic dicarboxylic acid, sulfophthalic acid or a sulfophthalic acid metal salt may be used. The sulfophthalic acid metal salt is a metal salt of sulfophthalic acid, and examples of the metal atom include alkali metal and alkaline earth metal.
Specifically, the sulfophthalic acid or the sulfophthalic acid metal salt is represented by the following formula (I) or (I'), respectively.

In the above formula (I'), M is a metal atom. n represents the valence of M.
Examples of the metal atom of M include alkali metals such as lithium, sodium and potassium, and alkaline earth metals such as beryllium, magnesium, calcium and strontium. Among them, alkali metals are preferable, sodium or lithium is preferable, and sodium is more preferable. When n is 2 or more, it can be crosslinked with another unit (for example, a sulfo group in another sulfophthalic acid unit or a sulfophthalic acid metal salt unit) via M.

In the above formulas (I) and (I'), ^RA is a substituted or unsubstituted alkyl group or a substituted or unsubstituted aryl group. m represents an integer of 0 to 3. When m is 2 or 3, each ^RA may be the same or different.
Examples of the alkyl group include a methyl group, an ethyl group, an n-propyl group, an isopropyl group, an n-butyl group, a t-butyl group, an n-octyl group, a 2-ethylhexyl group and the like. Among these, an alkyl group having 1 to 6 carbon atoms is preferable, and an alkyl group having 1 to 4 carbon atoms is more preferable.
Examples of the aryl group include a phenyl group and a naphthyl group. Among these, an aryl group having 6 to 12 carbon atoms is preferable, and a phenyl group is more preferable.
Examples of the substituent that the alkyl group and the aryl group may have include a halogen atom such as a chlorine atom, a bromine atom and an iodine atom, an alkyl group, an alkenyl group, an aryl group, a cyano group, a hydroxyl group, a nitro group and an alkoxy. Examples thereof include a group, an aryloxy group, an acyl group, an amino group, a mercapto group, an alkylthio group, an arylthio group and the like. Among these groups, those having a hydrogen atom may be further substituted with the above-mentioned substituent.

Specific examples of ^RA include methyl group, ethyl group, n-propyl group, isopropyl group, n-butyl group, t-butyl group, 1-methylpropyl group, 2-methylpropyl group, hydroxymethyl group, 1-. Examples thereof include hydroxyethyl group, mercaptomethyl group, methylthioethyl group, phenyl group, naphthyl group, biphenyl group, benzyl group and 4-hydroxybenzyl group, and among them, methyl group, ethyl group and benzyl group are preferable.

In the above formulas (I) and (I'), ^RB represents a hydrogen atom or an alkyl group having 1 to 4 carbon atoms.

The preferred ^RA is as described above, but the sulfophthalic acid or the sulfophthalic acid metal salt used in the polyester resin (X) has m = 0, that is, the benzene ring is not substituted with ^RA , respectively, as described below. The unit represented by the formula (Ia) or (I'a) is preferable.

In the above formula (Ia), ^RB is the same as ^RB in the above formula (I).
Further, in the above formula (I'a), RB, ^M , and n are the same as RB, ^M , and n in the above formula (I').

Further, as the sulfophthalic acid represented by the formula (Ia) or the sulfophthalic acid metal salt represented by the formula (I'a), the phthalic acid structure in which two -CO- are bonded to the ortho position, the meta position. Examples thereof include an isophthalic acid structure bonded to and a terephthalic acid structure bonded to the para position, and the isophthalic acid structure is particularly preferable. That is, it is preferably at least one of the sulfoisophthalic acid represented by the following formula (Ib) and the sulfoisophthalic acid metal salt represented by the following formula (I'b).

In the above formula (Ib), ^RB is the same as ^RB in the above formula (I).
In the above formula (I'b), RB, ^M , and n are the same as RB, ^M , and n in the above formula (I').

The position of the sulfo group in the sulfoisophthalic acid or the sulfoisophthalic acid metal salt can be 2, 4, 5, or 6, but is replaced with the 5-position represented by the following formula (Ic) or (I'c). It is preferable that it is.

In the above formula (Ic), ^RB is the same as ^RB in the above formula (I).
In the above formula ( ^I'c ), RB, M and n are the same as RB, ^M and n in the above formula (I').

In the polyester resin (X), examples of the sulfoisophthalic acid or sulfoisophthalic acid metal salt represented by the formula (Ic) or the formula (I'c) include 5-sulfoisophthalic acid and 5-sulfoisophthalic acid. Examples thereof include lithium 5-sulfoisophthalate, potassium 5-sulfoisophthalate, calcium bis (5-sulfoisophthalic acid), dimethylsodium 5-sulfoisophthalate, diethylsodium 5-sulfoisophthalate and the like.

When the polyester resin (X) contains a structural unit derived from at least one selected from the group consisting of sulfophthalic acid and a sulfophthalic acid metal salt, it is preferable to contain at least a structural unit derived from the sulfophthalic acid metal salt. The content of the structural unit derived from the sulfophthalic acid and the sulfophthalic acid metal salt in the polyester resin is preferably 0.01 to 15 mol%, more preferably 0.03 to 10 mol% of the entire structural unit derived from the dicarboxylic acid. It is 0.0 mol%, more preferably 0.06 to 5.0 mol%, and even more preferably 0.08 to 2.0 mol%.

Examples of the alicyclic dicarboxylic acid include cyclohexanedicarboxylic acid, norbornenedicarboxylic acid and tricyclodecanedicarboxylic acid.
Examples of the aliphatic dicarboxylic acid include malonic acid, succinic acid, adipic acid, azelaic acid, sebacic acid and the like.

Examples of the diol unit include a structural unit derived from an aliphatic diol, a structural unit derived from an alicyclic diol, and a structural unit derived from an aromatic diol, and a structural unit derived from an aliphatic diol is preferable.
Examples of the aliphatic diol include ethylene glycol, 2-butene-1,4-diol, trimethylene glycol, tetramethylene glycol, hexamethylene glycol, neopentyl glycol, methylpentanediol and diethylene glycol. Of these, ethylene glycol is preferred.
Examples of the alicyclic diol include cyclohexanedimethanol, isosorbide, spiroglycol, 2,2,4,4-tetramethyl-1,3-cyclobutanediol, norbornenedimethanol and tricyclodecanedimethanol.
Examples of the aromatic diol include bisphenol compounds and hydroquinone compounds.

The polyester resin (X) may have a structural unit derived from hydroxycarboxylic acid.
Examples of the hydroxycarboxylic acid include an aliphatic hydroxycarboxylic acid, an alicyclic hydroxycarboxylic acid, and an aromatic hydroxycarboxylic acid.
Examples of the aliphatic hydroxycarboxylic acid include 10-hydroxyoctadecanoyl acid, lactic acid, hydroxyacrylic acid, 2-hydroxy-2-methylpropionic acid, hydroxybutyl acid and the like.
Examples of the alicyclic hydroxycarboxylic acid include hydroxymethylcyclohexanecarboxylic acid, hydroxymethylnorbornenecarboxylic acid and hydroxymethyltricyclodecanecarboxylic acid.
Examples of the aromatic hydroxycarboxylic acid include hydroxybenzoic acid, hydroxytoluic acid, hydroxynaphthic acid, 3- (hydroxyphenyl) propionic acid, hydroxyphenyl acetic acid, 3-hydroxy-3-phenylpropionic acid and the like.

The polyester resin (X) may have a structural unit derived from a monofunctional compound and a structural unit derived from a polyfunctional compound.
Examples of the monofunctional compound include monocarboxylic acid and monoalcohol, and specifically, aromatic monocarboxylic acid, aliphatic monocarboxylic acid, aromatic monoalcohol, aliphatic monoalcohol, alicyclic monoalcohol and the like. Can be mentioned.
Examples of the polyfunctional compound include aromatic polycarboxylic acids, alicyclic polycarboxylic acids, aliphatic polyhydric alcohols, alicyclic polyhydric alcohols, and esters thereof.

The polyester resin (X) preferably has a constituent unit derived from a dicarboxylic acid containing a constituent unit derived from terephthalic acid and a constituent unit derived from a diol containing a constituent unit derived from ethylene glycol, and is preferably terephthalic acid. It is more preferable to have a constituent unit derived from a dicarboxylic acid containing 80 mol% or more of a constituent unit derived from an acid and a constituent unit derived from a diol containing 80 mol% or more of a constituent unit derived from ethylene glycol. It is more preferable to have a constituent unit derived from a dicarboxylic acid containing 90 mol% or more of a constituent unit derived from terephthalic acid and a constituent unit derived from a diol containing 90 mol% or more of a constituent unit derived from ethylene glycol. , Having a constituent unit derived from a dicarboxylic acid containing 98 mol% or more of a constituent unit derived from terephthalic acid, and a constituent unit derived from a diol containing substantially 100 mol% of a constituent unit derived from ethylene glycol. Is even more preferable.
Specific examples of the polyester resin (X) include polyethylene terephthalate (PET).

Polyethylene terephthalate (PET) may contain a structural unit derived from an aromatic dicarboxylic acid other than terephthalic acid. The aromatic dicarboxylic acid other than terephthalic acid is preferably one or more selected from isophthalic acid, orthophthalic acid, naphthalenedicarboxylic acid, and 4,4'-biphenyldicarboxylic acid. These are low in cost, and the copolymerized polyester resin containing them is easy to manufacture.
Of these, isophthalic acid and naphthalenedicarboxylic acid are preferable, and isophthalic acid is more preferable. Polyethylene terephthalate containing a structural unit derived from isophthalic acid is excellent in moldability and in that it prevents whitening of the molded product by slowing the crystallization rate. In addition, polyethylene terephthalate containing a structural unit derived from naphthalenedicarboxylic acid raises the glass transition point of the resin, improves heat resistance, and absorbs ultraviolet rays, so it is suitable for manufacturing multi-layer containers that require resistance to ultraviolet rays. Suitable for use. As the naphthalene dicarboxylic acid, a 2,6-naphthalenedicarboxylic acid component is preferable because it is easy to produce and highly economical.
When polyethylene terephthalate contains a constituent unit derived from an aromatic dicarboxylic acid other than terephthalic acid, the proportion of the constituent unit derived from an aromatic dicarboxylic acid other than terephthalic acid is preferably 1 to 20 mol% of the dicarboxylic acid unit. It is more preferably to 10 mol%, further preferably 1 to 5 mol%.

The polyester resin (X) may be used alone or in combination of two or more.
The polyester resin (X) can be produced by a known method such as a direct esterification method or a transesterification method.

The intrinsic viscosity of the polyester resin (X) is preferably 0.5 to 2.0 dL / g, more preferably 0.6 to 1.5 dL / g. When the intrinsic viscosity is 0.5 dL / g or more, the mechanical properties of the container are excellent.
The intrinsic viscosity is 0.2, 0.4, 0.6 g / dL solution by dissolving polyester resin in a mixed solvent of phenol / 1,1,2,2-tetrachloroethane (= 6/4 mass ratio). Is prepared and measured at 25 ° C. by an automatic viscosity measuring device (manufactured by Malvern, Viscotek).

(Other ingredients)
The polyester layer may contain other components. Examples of other components include heat stabilizers, light stabilizers, moisture proofing agents, waterproofing agents, lubricants, spreading agents and the like.
The polyester layer may contain a resin other than the polyester resin (X), which is the main component, as long as the effects of the present invention are not impaired. The content of the polyester resin (X) is preferably 80 to 100% by mass, more preferably 90 to 100% by mass, based on the amount of the resin in the entire polyester layer.

<Polyamide layer>
The polyamide layer contains a polyamide resin (Y), a yellowing inhibitor (A) and an oxidation accelerator (B). Further, the content of the polyamide resin (Y) contained in the polyamide layer is 0.05 to 7.0% by mass with respect to the total amount of all the polyamide layers and all polyester layers, and the yellowing inhibitor (A). Is a dye, and the content of the yellowing inhibitor (A) is 1 to 30 ppm with respect to the total amount of all the polyamide layers and all polyester layers.
By providing the polyamide layer, the multilayer container has a high oxygen barrier property. In the present invention, by further containing the oxidation accelerator (B) and the yellowing inhibitor (A) which is a dye in the polyamide layer, extremely high oxygen barrier properties and the yellowing suppression of the recycled polyester produced from the multilayer container are suppressed. Can be compatible with each other.
The reason for exhibiting such an excellent effect is not clear, but it is considered as follows.
In the present invention, yellowing can be effectively suppressed by including the yellowing inhibitor (A) in the polyamide layer containing nitrogen, which tends to cause yellowing of the recycled resin. However, when these yellowing inhibitors coexist with the oxidation promoter, oxygen absorption by the oxidation promoter is inhibited. In the present invention, a specific amount of a dye that does not easily inhibit the oxidation reaction is used as the yellowing inhibitor, and the dye is contained in the polyamide layer together with the oxidation accelerator to exhibit effective yellowing inhibitory performance and oxygen absorption capacity. It is thought that it can be enhanced.

(Polyamide resin (Y))
Examples of the polyamide resin (Y) include a xylylene group-containing polyamide resin, nylon 6, nylon 66, nylon 666, nylon 610, nylon 11, nylon 12, and a mixture thereof. Among these, a xylylene group-containing polyamide resin is preferable because it can improve the gas barrier performance and can be easily separated from the polyester layer during recycling. The xylylene group-containing polyamide resin is preferably a polyamide resin containing a structural unit derived from xylylenediamine.

The xylylene group-containing polyamide resin is a polycondensation of a diamine containing xylylenediamine and a dicarboxylic acid, and has a structural unit derived from xylylenediamine and a structural unit derived from dicarboxylic acid. The xylylene group-containing polyamide resin preferably has 50 mol% or more, more preferably 70 mol% or more, and more preferably 80 mol% or more of the structural units derived from xylylenediamine among the structural units (diamine units) derived from diamine. It is more preferably contained in an amount of about 100 mol%, and even more preferably contained in an amount of 90 to 100 mol%.
As the xylylenediamine, metaxylylenediamine, paraxylylenediamine, or both are preferable, but metaxylylenediamine is more preferable. The diamine unit constituting the xylylene group-containing polyamide resin preferably contains 50 mol% or more, more preferably 70 mol% or more, and 80 to 100 mol% of the constituent unit derived from m-xylylenediamine. It is even more preferable to contain 90 to 100 mol%. When the constituent unit derived from m-xylylenediamine in the diamine unit is within the above range, the polyamide resin has better gas barrier properties.

The diamine unit in the xylylene group-containing polyamide resin may be composed of only a structural unit derived from xylylenediamine, but may contain a structural unit derived from a diamine other than xylylenediamine. Here, examples of diamines other than xylylene diamine include ethylenediamine, tetramethylenediamine, pentamethylenediamine, 2-methylpentanediamine, hexamethylenediamine, heptamethylenediamine, octamethylenediamine, nonamethylenediamine, decamethylenediamine, and dodecamethylene. An aliphatic diamine having a linear or branched structure such as diamine, 2,2,4-trimethyl-hexamethylenediamine, 2,4,4-trimethyl-hexamethylenediamine; 1,3-bis (aminomethyl) cyclohexane, 1 , 4-bis (aminomethyl) cyclohexane, 1,3-diaminocyclohexane, 1,4-diaminocyclohexane, bis (4-aminocyclohexyl) methane, 2,2-bis (4-aminocyclohexyl) propane, bis (aminomethyl) ) Alicyclic diamines such as decalin and bis (aminomethyl) tricyclodecane; diamines having an aromatic ring such as bis (4-aminophenyl) ether, paraphenylenediamine and bis (aminomethyl) naphthalene can be mentioned.

In the xylylene group-containing polyamide resin, examples of the compound that can constitute a dicarboxylic acid unit include succinic acid, glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, undecanedioic acid, and dodecanedioic acid. 4 to 20 α, ω-linear aliphatic dicarboxylic acids; alicyclic dicarboxylic acids such as 1,4-cyclohexanedicarboxylic acid; other aliphatic dicarboxylic acids such as dimer acid; terephthalic acid, isophthalic acid, orthophthalic acid , Xylylene dicarboxylic acid, aromatic dicarboxylic acid such as naphthalenedicarboxylic acid, etc., α, ω-linear aliphatic dicarboxylic acid having 4 to 20 carbon atoms is preferable, adipic acid and sebacic acid are more preferable, and barrier. Adipic acid is more preferable from the viewpoint of improving the performance.
The xylylene group-containing polyamide resin preferably contains 50 mol% or more, more preferably 70 mol% or more, of the constituent units derived from dicarboxylic acid (dicarboxylic acid units). It is more preferably contained in an amount of 80 to 100 mol%, and even more preferably contained in an amount of 90 to 100 mol%.

That is, the polyamide resin (Y) is derived from a diamine-derived structural unit containing 50 mol% or more of a structural unit derived from xylylenediamine and a dicarboxylic acid containing 50 mol% or more of adipic acid-derived structural unit. It is preferable to have a structural unit derived from a diamine containing 80 mol% or more of a structural unit derived from xylylenediamine, and a dicarboxylic acid containing 80 mol% or more of a structural unit derived from adipic acid. It is more preferable to have a constituent unit from which it is derived.
As the xylylenediamine, metaxylylenediamine is preferable.
Further, as the remaining dicarboxylic acid unit excluding adipic acid, a structural unit derived from α, ω-linear aliphatic dicarboxylic acid having 4 to 20 carbon atoms is preferable.

Further, as a preferable xylylene group-containing polyamide resin, 70 mol% or more of the diamine unit is a constituent unit derived from xylylenediamine (preferably methylylenediamine), and 70 to 99 mol% of the dicarboxylic acid unit is adipic acid. It is also possible to exemplify a polyamide resin which is a constituent unit derived from is and 1 to 30 mol% is a constituent unit derived from isophthalic acid. In the polyamide resin, 80 mol% or more of the diamine unit is a structural unit derived from m-xylylenediamine (preferably methylylenediamine), and 80 to 99 mol% of the dicarboxylic acid unit is a structural unit derived from adipic acid. It is preferable that the polyamide resin is 1 to 20 mol% of which is a constituent unit derived from isophthalic acid.
By adding an isophthalic acid unit as a dicarboxylic acid unit, the melting point can be lowered and the molding processing temperature can be lowered, so that thermal deterioration during molding can be suppressed, and the stretchable formability can be improved by delaying the crystal time. improves.

In addition to the above-mentioned diamine and dicarboxylic acid, lactams such as ε-caprolactam and laurolactam, aminocaproic acid, aminoundecanoic acid and the like can be used as components constituting the xylylene group-containing polyamide resin as long as the effects of the present invention are not impaired. Aliphatic aminocarboxylic acids; aromatic aminocarboxylic acids such as p-aminomethylbenzoic acid can also be used as the copolymerization component.

The xylylene group-containing polyamide resin is preferably produced by a polycondensation reaction in a molten state (hereinafter, may be referred to as “molten polycondensation”). For example, it is preferable to produce a nylon salt composed of a diamine and a dicarboxylic acid by a method of heating the temperature in the presence of water by a pressure method and polymerizing in a molten state while removing water. Further, it may be produced by a method in which diamine is directly added to a molten dicarboxylic acid and polycondensed under normal pressure. In this case, in order to keep the reaction system in a uniform liquid state, diamine is continuously added to the dicarboxylic acid, during which the reaction temperature is raised so that the reaction temperature does not fall below the melting points of the oligoamide and polyamide produced. However, it is preferable to proceed with polycondensation. Further, the xylylene group-containing polyamide can be increased in molecular weight by further solid-phase polymerization of the polyamide obtained by melt polycondensation, if necessary.

The xylylene group-containing polyamide resin is preferably polycondensed in the presence of a phosphorus atom-containing compound. When the xylylene group-containing polyamide resin is polycondensed in the presence of a phosphorus atom-containing compound, the processing stability during melt molding is enhanced and coloring is easily suppressed.
As the phosphorus atom-containing compound, a hypophosphoric acid compound and a hypophosphoric acid compound are preferable, and a hypophosphoric acid compound is more preferable.
The phosphorus atom-containing compound is preferably an organic metal salt, and more preferably an alkali metal salt.

Examples of the hypophosphorous acid compound include hypophosphorous acid, hypophosphorous acid metal salt, phenyl subphosphorous acid metal salt, ethyl hypophosphorous acid, and dimethylphosphinic acid from the viewpoint of promoting the polymerization reaction and preventing coloration. Examples thereof include phenylmethylphosphinic acid, phenyl subphosphonic acid, ethyl phenyl subphosphonate and the like, and a metal salt of hypophosphorous acid is preferable.
Examples of the hypophosphite metal salt include sodium hypophosphite, potassium hypophosphite, lithium hypophosphite, calcium hypophosphite, and sodium hypophosphite is more preferable.
Examples of the phenyl subphosphonate metal salt include sodium phenyl subphosphonate, potassium phenyl subphosphonate, and lithium phenyl subphosphonate.

Phosphorous acid compounds include phosphorous acid, pyrophosphite, metal phosphite, metal phenylphosphonic acid, triethyl phosphite, triphenyl phosphite, ethylphosphonic acid, phenylphosphonic acid, and phenylphosphonic acid. Examples thereof include diethyl and the like.
Examples of the metal phosphite salt include sodium hydrogenphosphite, sodium phosphite, potassium phosphite, calcium phosphite and the like.
Examples of the phenylphosphonate metal salt include sodium ethylphosphonate, potassium ethylphosphonate, sodium phenylphosphonate, potassium phenylphosphonate, lithium phenylphosphonate and the like.
The phosphorus atom-containing compound may be used alone or in combination of two or more.

Further, the polycondensation of the xylylene group-containing polyamide resin is preferably performed in the presence of a phosphorus atom-containing compound and an alkali metal compound. If the amount of the phosphorus atom-containing compound used is large, the polyamide resin may gel. Therefore, from the viewpoint of adjusting the amidation reaction rate, it is preferable to allow the alkali metal compound to coexist.
Examples of the alkali metal compound include alkali metal hydroxides and alkali metal acetates. Examples of the alkali metal hydroxide include lithium hydroxide, sodium hydroxide, potassium hydroxide, rubidium hydroxide and cesium hydroxide, and examples of the alkali metal acetate include lithium acetate, sodium acetate, potassium acetate and rubidium acetate. Examples include cesium acetate.
When an alkali metal compound is used when polycondensing a polyamide resin, the amount of the alkali metal compound used is obtained by dividing the number of moles of the alkali metal compound by the number of moles of the phosphorus atom-containing compound from the viewpoint of suppressing gel formation. The value is preferably 0.5 to 1, more preferably 0.55 to 0.95, and even more preferably 0.6 to 0.9.

The number average molecular weight of the polyamide resin is appropriately selected depending on the use and molding method of the multilayer container, but is preferably 10,000 to 60,000, preferably 11,000 to 50,000, from the viewpoint of moldability and strength of the multilayer container. Is more preferable.
The number average molecular weight of the polyamide resin is calculated from the following formula (X).
Number average molecular weight = 2 × 1,000,000 / ([COOH] + [NH ₂ ]) ... (X)
(In the formula, [COOH] represents the terminal carboxyl group concentration (μmol / g) in the polyamide resin, and [NH ₂ ] represents the terminal amino group concentration (μmol / g) in the polyamide resin.)
Here, the terminal amino group concentration is a value calculated by neutralizing and titrating a polyamide resin in a phenol / ethanol mixed solution with a dilute aqueous hydrochloric acid solution, and the terminal carboxyl group concentration is a polyamide resin dissolved in benzyl alcohol. Use the value calculated by neutralizing and titrating with an aqueous solution of sodium hydroxide.

The content of the polyamide resin (Y) contained in the polyamide layer is 0.05 to 7.0% by mass with respect to the total amount of all the polyamide layers and all polyester layers, and has gas barrier properties and suppresses yellowing of recycled polyester. From the viewpoint of the above, 0.5 to 6.0% by mass is preferable, 1.0 to 5.0% by mass is more preferable, and 1.5 to 4.5% by mass is further preferable.

(Yellowing inhibitor (A))
The polyamide layer of the multilayer container contains a yellowing inhibitor (A), and the yellowing inhibitor (A) is a dye, and the content thereof is 1 with respect to the total amount of all polyamide layers and all polyester layers. ~ 30 ppm.
The content of the yellowing inhibitor (A) is 1 to 30 ppm with respect to the total amount of the total polyamide layer and the total polyester layer, and from the viewpoint of effectively suppressing the yellowing of the regenerated polyester, 1.5 to 25 ppm is preferable, 2 to 22 ppm is more preferable, 3 to 20 ppm is further preferable, and 8 to 20 ppm is further preferable from the viewpoint of mixability and moldability during production.
In the present invention, "ppm" is a parts per million by mass.
The content of the yellowing inhibitor (A) is preferably 0.001 to 1.0% by mass, preferably 0.005 to 0.5% by mass in the polyamide layer from the viewpoint of effectively suppressing the yellowing of the regenerated polyester. % Is more preferable, 0.008 to 0.1% by mass is further preferable, 0.01 to 0.08% by mass is further preferable, and 0.03 to 0.08% by mass is further preferable.

The yellowing inhibitor (A) is a dye from the viewpoint of transparency, and a blue dye is particularly preferable.
By using a dye, it is possible to suppress the yellowing of the recycled polyester obtained from the multilayer container of the present invention in an extremely small amount. In addition, recycled polyester having excellent transparency can be obtained.

Examples of the dye include anthraquinone dyes, pyrazolone dyes, coumarin dyes, perinone dyes, methine dyes, and quinophthalone dyes, and anthraquinone dyes are preferable.
Examples of the anthraquinone dye include an anthraquinone dye in which the hydrogen atom of the aromatic ring is substituted with an aromatic amine, an aliphatic amine and a halogen, and an anthraquinone dye in which a hydrogen atom of the aromatic ring is substituted with an aromatic amine. preferable. By using such an anthraquinone dye, yellowing of the regenerated polyester can be suppressed. As the anthraquinone dye, an anthraquinone dye in which the hydrogen atom of the aromatic ring is not substituted with a hydroxyl group is preferable. By using such an anthraquinone dye, a high oxygen barrier property can be obtained in the multilayer container of the present invention.
By using an anthraquinone dye, it is possible to suppress the yellowing of the recycled polyester obtained from the multilayer container of the present invention in an extremely small amount.
The anthraquinone-based dye is more preferably an anthraquinone-based blue dye.
As the anthraquinone dye, a compound represented by the following formula (1) is preferable.

（式中、ｎはＲの数を表し、２つのｎはそれぞれ独立して１～５である。２ｎ個のＲはそれぞれ独立して炭素数１～４のアルキル基を示す。）

(In the formula, n represents the number of R, and the two n are independently 1 to 5. 2n R each independently represents an alkyl group having 1 to 4 carbon atoms.)

In the formula (1), n is 1 to 5, preferably 2 to 5, and more preferably 2 to 3. By setting n in the above range, yellowing (Δb ^* value) of the regenerated polyester can be suppressed. Each R independently represents an alkyl group having 1 to 4 carbon atoms, and is preferably at least one selected from the group consisting of a methyl group and an ethyl group. It is preferable that R is substituted with at least the ortho-position or the para-position with respect to the amino group, preferably at least the para-position is substituted, more preferably at least the ortho-position is substituted, and the ortho-position is substituted. And it is more preferable to replace the para position.
Specific examples of the compound represented by the formula (1) include 1,4-bis [(2-ethyl-6-methylphenyl) amino] anthraquinone, Solvent Blue 97, Solvent Blue 104, and Solvent Green 3. 4-bis [(2-ethyl-6-methylphenyl) amino] anthraquinone, Solvent Blue 97, Solvent Blue 104 are preferable.

Commercially available products of the yellowing inhibitor (A) include MACROLLEX Blue 3R (1,4-bis [(2-ethyl-6-methylphenyl) amino] anthraquinone, anthraquinone dye, manufactured by LANXESS), MACROLLEX Blue RR Gran ( Anthraquinone dyes (manufactured by LANXESS), Organet Blue 690 (anthraquinone dyes, manufactured by BASF), Quinizarin Green SS (anthraquinone dyes, manufactured by Tokyo Kasei Kogyo Co., Ltd.) and the like can be mentioned.

(Pro-oxidant (B))
In the multilayer container of the present invention, the polyamide layer contains an oxidation accelerator (B) for the purpose of inducing an oxidation reaction of the polyamide resin (Y) to enhance the oxygen absorption function and further enhance the gas barrier property.
The oxidation accelerator (B) is preferably a compound containing a transition metal, and more preferably at least one selected from the group consisting of a transition metal alone, an oxide, an inorganic acid salt, an organic acid salt, and a complex. preferable.
Examples of the inorganic acid salt include halides such as chlorides and bromides, carbonates, sulfates, nitrates, phosphates, silicates and the like.
Examples of the organic acid salt include carboxylates, sulfonates, phosphonates and the like.
Examples of the complex include a complex with β-diketone, β-keto acid ester and the like.

As the transition metal, a transition metal of Group VIII of the Periodic Table of the Elements is preferable, and at least one selected from the group consisting of cobalt, iron, manganese, and nickel is more preferable from the viewpoint of exhibiting oxygen absorption ability, and cobalt is more preferable. Is more preferable.

From the viewpoint of satisfactorily expressing the oxygen absorbing ability, among the compounds containing transition metals, specifically, from the group consisting of carboxylates containing transition metals, carbonates, acetylacetonate complexes, oxides and halides. At least one selected is preferred, at least one selected from octanate, neodecanoate, naphthenate, stearate, acetate, carbonate and acetylacetonate complexes is more preferred, cobalt octanoate, cobalt naphthenate, Cobalt carboxylates such as cobalt acetate, cobalt neodecanoate, and cobalt stearate are more preferred.

As the oxidation accelerator (B), one type may be used alone, or two or more types may be used in combination.
The content of the oxidation accelerator (B) is preferably 0.0001 to 1.0% by mass with respect to the polyamide layer from the viewpoint of enhancing the gas barrier property and suppressing the yellowing of the recycled polyester resin. It is more preferably 0.01 to 0.8% by mass, and even more preferably 0.05 to 0.6% by mass.
Further, the content of the oxidation accelerator (B) is preferably 0.0001 to 100 parts by mass of the polyamide resin (Y) from the viewpoint of enhancing the gas barrier property and suppressing the yellowing of the recycled polyester resin. It is 1.0 part by mass, more preferably 0.01 to 0.8 part by mass, and further preferably 0.05 to 0.6 part by mass.
Further, the content of the transition metal of the oxidation accelerator (B) is preferably 0.00001 to 0.1 with respect to the polyamide layer from the viewpoint of enhancing the gas barrier property and suppressing the yellowing of the recycled polyester resin. It is by mass, more preferably 0.0001 to 0.08% by mass, still more preferably 0.0003 to 0.06% by mass.
Further, the content of the transition metal of the oxidation accelerator (B) is preferably 0 with respect to 100 parts by mass of the polyamide resin (Y) from the viewpoint of enhancing the gas barrier property and suppressing the yellowing of the recycled polyester resin. It is .00001 to 0.1 parts by mass, more preferably 0.0001 to 0.08 parts by mass, and further preferably 0.0003 to 0.06 parts by mass. When a carboxylate containing a transition metal or the like is used as the oxidation accelerator (B), the content of the transition metal means the content of the transition metal itself in the compound containing the transition metal. ..

(Greening inhibitor (C))
The polyamide layer of the multilayer container preferably contains the greening inhibitor (C).
The greening inhibitor (C) suppresses the green color in the −a ^* direction as measured by a color difference meter when the multilayer container of the present invention is recycled into recycled polyester.
The content of the greening inhibitor (C) is 1 to 30 ppm with respect to the total amount of the total polyamide layer and the total polyester layer, and from the viewpoint of effectively suppressing the greening of the regenerated polyester, 1.5 to 25 ppm is preferable, 2 to 22 ppm is more preferable, and 3 to 20 ppm is further preferable from the viewpoint of mixability and moldability during production.
In the present invention, "ppm" is a parts per million by mass.
The content of the greening inhibitor (C) is preferably 0.001 to 1.0% by mass, preferably 0.005 to 0.5% by mass in the polyamide layer from the viewpoint of effectively suppressing the greening of the regenerated polyester. % Is more preferable, 0.008 to 0.1% by mass is further preferable, and 0.01 to 0.08% by mass is further preferable.

The mass ratio [(A) / (C)] of the yellowing inhibitor (A) and the greening inhibitor (C) in the polyamide layer of the multilayer container of the present invention is preferably 20/80 to 80/20. , More preferably 30/70 to 70/30, and even more preferably 40/60 to 60/40.
When the mass ratio is in this range, the hue change of the recycled polyester obtained after recycling becomes small, and a polyester having particularly excellent colorlessness can be obtained.

The greening inhibitor (C) is preferably a dye from the viewpoint of transparency.
Among the dyes, at least one selected from the group consisting of anthraquinone dyes and azo dyes is preferable, and anthraquinone dyes are more preferable from the viewpoint of heat resistance.
As the anthraquinone dye, an anthraquinone dye in which the hydrogen atom of the aromatic ring is not substituted with a hydroxyl group is preferable. By using such an anthraquinone dye, high oxygen gas barrier property can be obtained in the multilayer container of the present invention.
Further, the greening inhibitor (C) is preferably a red dye, more preferably at least one selected from the group consisting of anthraquinone-based red dyes and azo-based red dyes, and from the viewpoint of heat resistance. Anthraquinone-based red dyes are even more preferred.
By using the anthraquinone-based red dye and the azo-based red dye, it is possible to suppress the greening of the recycled polyester obtained from the multilayer container of the present invention in an extremely small amount.
As the anthraquinone dye, a compound represented by the following formula (2) is preferable.

（式（２）中、２つのＹはそれぞれ独立して水素原子又は式（２ａ）で示される基を表す。ただし、少なくとも１つのＹは式（２ａ）で示される基である。
式（２ａ）中、Ｒは炭素数１～４のアルキル基を示す。）

(In the formula (2), the two Ys independently represent a hydrogen atom or a group represented by the formula (2a), where at least one Y is a group represented by the formula (2a).
In formula (2a), R represents an alkyl group having 1 to 4 carbon atoms. )

In the formula (2), the two Ys independently represent a hydrogen atom or a group represented by the formula (2a), but at least one Y is a group represented by the formula (2a) and one Y represents the formula (2a). It is preferable that the group represented by (2a) has the remaining Y being a hydrogen atom.
In the formula (2a), R represents an alkyl group having 1 to 4 carbon atoms, and is preferably at least one selected from the group consisting of a methyl group and an ethyl group. When the two Ys are the groups represented by the formula (2a), the Rs in the groups represented by the two formulas (2a) may be the same or different. It is preferable that R is substituted at the para position with respect to the amino group.
Specific examples of the compound represented by the formula (2) include Solvent Violet 36 and the like.
The greening inhibitor (B) may be used alone or in combination of two or more.

Commercially available products of the greening inhibitor (B) include MACROLEX Violet 3R Gran (anthraquinone dye, manufactured by LANXESS), MACROLEX Red Violet R Gran (Disperse Violet 31, Disperse Violet 26, SolvenTra) and Solven MACROLEX Red 5B Gran (Disperse Violet 31, Disperse Violet 26, Solvent Violet 59, anthraquinone dye, LANXESS), MACROLEX Red B (Solvent Red 195, azo dye, LAN).

(Polyester resin (Z))
The polyamide layer of the multilayer container preferably contains a polyester resin (Z) from the viewpoint of suppressing yellowing of the recycled polyester and improving the impact resistance.
The polyester resin (Z) used for the polyamide layer is preferably the polyester resin described in the section (Polyester resin (X)) contained in the polyester layer, and the same applies to suitable polyester resins.
Specifically, the polyester resin (Z) is preferably polyethylene terephthalate (PET). The polyethylene terephthalate may contain a structural unit derived from an aromatic dicarboxylic acid other than terephthalic acid, and the structural unit derived from an aromatic dicarboxylic acid other than terephthalic acid is preferably a structural unit derived from sulfophthalic acid or a sulfophthalic acid metal salt. .. The sulfophthalic acid metal salt is a metal salt of sulfophthalic acid, and examples of the metal atom include alkali metal and alkaline earth metal.
By including the polyester resin (Z) in the polyamide layer, the yellowing of the recycled polyester obtained by recycling is suppressed, and the adhesiveness between the polyamide layer and the polyester layer is improved, so that the impact resistance of the multilayer container is good. Become.

(Other ingredients)
The polyamide layer may contain other components. Examples of other components include heat stabilizers, light stabilizers, moisture proofing agents, waterproofing agents, lubricants, spreading agents and the like.
The polyamide layer may contain a resin other than the polyamide resin (Y) which is the main component, as long as the effect of the present invention is not impaired.
In particular, when the yellowing inhibitor (A) is mixed using the masterbatch method described later, it is preferable to contain the polyamide resin or polyester resin used in the masterbatch. In that case, the polyamide resin or polyester resin used in the masterbatch is preferably 1 to 20% by mass, more preferably 3 to 15% by mass, based on the total amount of the resin in the polyamide layer.

(Resin composition in the polyamide layer)
The content of the polyamide resin (Y) in the polyamide layer is preferably 80 to 100% by mass, more preferably 90 to 100% by mass, based on the total amount of the resin in the polyamide layer from the viewpoint of gas barrier properties.
When the polyester resin (Z) is contained in the polyamide layer, the content of the polyester resin (Z) in the polyamide layer is preferably 5 to 70% by mass, preferably 10 to 65, from the viewpoint of impact resistance and gas barrier properties. The mass% is more preferable, 20 to 65% by mass is further preferable, and 40 to 65% by mass is further preferable. When the content of the polyester resin (Z) is within the above range, the multilayer container of the present invention suppresses yellowing of the recycled polyester obtained by recycling, improves the adhesiveness between the polyamide layer and the polyester layer, and is resistant to the yellowing. Impact resistance is good.

<Structure and characteristics of multi-layer container>
The multilayer container of the present invention has a multilayer structure having a polyester layer containing a polyester resin (X) and a polyamide layer containing a polyamide resin (Y), a yellowing inhibitor (A) and an oxidation accelerator (B). ing.
The multilayer container of the present invention may contain the polyester layer and a resin layer other than the polyamide layer, but the polyester layer and the above may be contained from the viewpoint of facilitating sorting at the time of recycling and improving the yellowing suppressing effect. The content of the resin layer other than the polyamide layer is preferably small, and it is preferable that the polyester layer and the resin layer other than the polyamide layer are substantially not contained. Further, an adhesive layer made of an adhesive or an inorganic layer made of an inorganic substance may be provided, but these are also made of the adhesive layer or the inorganic layer from the viewpoint of facilitating separation at the time of recycling and improving the yellowing suppressing effect. The content is preferably low, and it is preferable that the adhesive layer and the inorganic layer are not substantially contained.

The multi-layer container of the present invention has a multi-layer structure of two or more layers, preferably has a 2- to 5-layer structure, more preferably has a 3- to 5-layer structure, and has a 3-layer structure or a 5-layer structure. Is even more preferable, and it is even more preferable to have a three-layer structure.
The outermost layer of the multilayer container of the present invention is preferably a polyester layer. Further, the innermost layer is preferably a polyester layer, and the outermost layer and the innermost layer are more preferably polyester layers.
When the outermost layer is a polyester layer, the multilayer container has excellent impact resistance, appearance, and design.
Therefore, as the structure of the multi-layer container, it is preferable that the multi-layer container has a 2 to 5 layer structure and the outermost layer is a polyester layer, the multi-layer container has a 3 to 5 layer structure, and the outermost layer and the innermost layer are. A polyester layer is more preferable.

In the case of a two-layer structure, the innermost layer is preferably a polyamide layer / polyester layer, and in the case of a three-layer structure, the innermost layer is preferably a polyester layer / polyamide layer / polyester layer, and in the case of a five-layer structure. From the innermost layer, a polyester layer / polyamide layer / polyester layer / polyamide layer / polyester layer is preferable.

The multi-layer container of the present invention is preferably a hollow container, and when the multi-layer container is a hollow container, the body portion has at least a multi-layer structure. The ratio (thickness ratio W / S) of the thickness (W) of the polyester layer to the thickness (S) of the polyamide layer in the body is preferably 2.5 or more and 200 or less. The thickness of the polyester layer means an average thickness, and when there are a plurality of polyester layers in the body, the thickness of the plurality of layers is averaged to obtain the average thickness per layer. Is. The thickness of the polyamide layer is the same.
When the thickness ratio W / S is 2.5 or more, the polyamide resin is easily separated from the polyester resin in the separation step in the method for producing a recycled polyester, particularly in the wind selection separation and the specific gravity separation, which is preferable. Further, when the thickness ratio W / S is 200 or less, the gas barrier property of the hollow container is excellent, and the contents can be stored for a long period of time.
From the viewpoint of improving the gas barrier property of the hollow container while improving the sorting property in the sorting step, the thickness ratio (W / S) is more preferably 3 to 50, and further preferably 4 to 15.

When the multilayer container is a hollow container, the total thickness of the body of the hollow container (that is, the total thickness of all layers of the body) is preferably 100 μm to 5 mm, more preferably 150 μm to 3 mm, and more preferably 200 μm to 200 μm. 2 mm is more preferable. The thickness (W) of each polyester layer is preferably 30 μm to 2 mm, more preferably 40 μm to 1 mm, and even more preferably 50 μm to 500 μm. The thickness (S) of each polyamide layer is preferably 1 to 200 μm, more preferably 3 to 100 μm, and even more preferably 8 to 50 μm. In the present invention, by setting the thickness of the polyamide layer within this range, the polyamide layer can be easily separated from polyester in the separation step while ensuring the gas barrier property.

When the multilayer container is a hollow container, the polyamide layer is preferably present in 50% or more of the surface area of the outer surface of the container, and is present in 70% or more of the surface area of the outer surface of the container from the viewpoint of improving the gas barrier property. It is more preferably present in 90% or more of the surface area of the outer surface of the container, further preferably 99% or more of the surface area of the outer surface of the container, and substantially 100 of the surface area of the outer surface of the container. It is even more preferable to be present in%, and even more preferably to be present in 100% of the surface area of the outer surface of the container.

When the multilayer container of the present invention is a hollow container, it is more preferably a liquid packaging container used by filling the inside of the hollow container with a liquid, and further preferably a beverage packaging container. Examples of the liquid to be filled inside include beverages, liquid seasonings, chemicals, pharmaceuticals, detergents and the like, and beverages capable of effectively preventing deterioration due to oxygen by the multilayer container of the present invention are preferable.
Examples of the beverage include water, carbonated water, oxygenated water, hydrogen water, milk, dairy products, juice, coffee, coffee beverages, carbonated soft drinks, teas, alcoholic beverages and the like.
Examples of the liquid seasoning include sauces, soy sauce, syrups, mirins, dressings and the like.
Examples of chemical products include pesticides and pesticides.

The oxygen barrier property of the multi-layer container of the present invention can be evaluated by an oxygen permeability test by the MOCON method according to ASTM D3985. The oxygen permeability (cc / (bottle. When the layer hollow container is used, 0.020 or less is preferable, 0.010 or less is more preferable, and 0.005 or less is further preferable. The three-layer hollow container can be manufactured by the method of the embodiment.
OX-TRAN2 / 61 manufactured by MOCON was used for the measurement, 100 mL of water was filled in the 500 mL container, the temperature was 23 ° C., the internal humidity of the container was 100% RH, and the external humidity was under the condition of an oxygen partial pressure of 0.21 atm. At 50% RH, 1 atm of nitrogen is circulated inside the container at 20 mL / min, and the inside of the container is measured by detecting oxygen contained in the circulated nitrogen with a coulometric sensor.

[Manufacturing method of multi-layer container]
The method for producing the multilayer container of the present invention is not limited, but it is preferably produced by the following method.
The method for producing a multilayer container of the present invention has a polyester layer containing a polyester resin (X) and a polyamide layer containing a polyamide resin (Y), a yellowing inhibitor (A) and an oxidation accelerator (B). The content of the polyamide resin (Y) is 0.05 to 7.0% by mass with respect to the total amount of all polyamide layers and all polyester layers, and the yellowing inhibitor (A) is a dye and yellowing. A method for producing a multilayer container in which the content of the inhibitor (A) is 1 to 30 ppm with respect to the total amount of the total polyamide layer and the total polyester layer, wherein the polyamide resin (Y) and the yellowing inhibitor (A) are used. ) And the oxidation accelerator (B) to prepare a polyamide resin mixture 1. The polyamide resin mixture and the polyester resin composition containing the polyester resin (X) are co-injection molded to form a multilayer preform. It is preferable to include the step 2 for obtaining and the step 3 for blow-molding the multilayer preform.

<Step 1 (Step of preparing a polyamide resin mixture)>
In step 1, a polyamide resin (Y), a yellowing inhibitor (A), and an oxidation accelerator (B) are mixed to prepare a polyamide resin mixture.
Normally, in order to spread the yellowing inhibitor throughout the container, a facility for stirring and mixing or kneading the yellowing inhibitor and all the resins is required, but in the method for producing a multilayer container of the present invention, a small amount is required. By mixing the yellowing inhibitor (A) and the oxidation accelerator (B) with the polyamide resin (Y) in the above, the yellowing inhibitor is efficiently distributed throughout the container by mixing on a small scale and in a short time. It can be and is excellent in productivity.
The mixing method may be dry blending or melt blending (melt kneading), but dry blending or masterbatch method melt blending is preferable from the viewpoint of reducing the heat history and preventing deterioration of the resin and the yellowing inhibitor. .. Further, from the viewpoint of preventing the yellowing inhibitor from adhering to and remaining around the molding machine or the molding machine in step 2, the melt blend is preferable, and the heat history is reduced, and the resin and the yellowing inhibitor are deteriorated. The masterbatch method is preferable from the viewpoint of preventing the above.

In step 1, it is preferable to mix the pellet-shaped polyamide resin (Y), the yellowing inhibitor (A) and the oxidation accelerator (B) at 230 ° C. or lower, and more preferably at 150 ° C. or lower. It is more preferable to mix at 100 ° C. or lower. By mixing at 230 ° C. or lower, the heat history can be reduced and deterioration of the resin and the yellowing inhibitor can be prevented. It is considered that this is because the polyamide resin can maintain the pellet-like morphology, so that there is little thermal deterioration. When mixing at 230 ° C. or lower, it is preferable to perform a dry blend.
The yellowing inhibitor (A) preferably used in step 1 is the same as that described in the above section (yellowing inhibitor (A)), and is a dye, more preferably an anthraquinone dye. ..
The yellowing inhibitor (A) is preferably in the form of powder, dispersion or solution, and more preferably in the form of powder. When the yellowing inhibitor (A) is in these forms, it can be more easily and uniformly mixed with the polyamide resin (Y).
The oxidation-promoting agent (B) preferably used in step 1 is the same as that described in the above section (oxidation-promoting agent (B)). Specifically, it is preferably a compound containing a transition metal, and at least one selected from the group consisting of a carboxylate containing a transition metal, a carbonate, an acetylacetonate complex, an oxide and a halide is preferable, and octanoic acid is preferable. More preferably, at least one selected from salts, neodecanoates, naphthenates, stearate, acetates, carbonates and acetylacetonate complexes is preferred, including cobalt octanate, cobalt naphthenate, cobalt acetate, cobalt neodecanoate, stearic acid. Cobalt carboxylates such as cobalt are more preferred.

Further, in step 1, it is preferable to further mix the greening inhibitor (C).
The greening inhibitor (C) preferably used in step 1 is the same as that described in the above section (greening inhibitor (C)), and is at least one selected from the group consisting of dyes and pigments. It is preferably at least one selected from the group consisting of anthraquinone dyes and azo dyes, and more preferably at least one selected from the group consisting of anthraquinone red dyes and azo red dyes. It is even more preferable, and from the viewpoint of heat resistance, an anthraquinone-based red dye is even more preferable.
Further, the greening inhibitor (C) is preferably in the form of powder, dispersion or solution, and more preferably in the form of powder. When the greening inhibitor (C) is in these forms, it can be more easily and uniformly mixed with the polyamide resin (Y).

Further, in step 1, it is preferable to mix the polyester resin (Z).
The polyester resin (Z) preferably used in step 1 is the same as that described in the above section (polyester resin (Z)). When mixing by dry blending, the polyester resin (Z) is preferably mixed in the form of pellets.

Examples of the mixing device used for dry blending include a tumbler mixer, a ribbon mixer, a Henschel mixer, a Banbury mixer and the like.

Examples of the method for mixing the polyamide resin (Y), the yellowing inhibitor (A) and the oxidation accelerator (B) in the melt blend in step 1 include a masterbatch method and a full compound method, and the masterbatch method is preferable. ..
The masterbatch method is a method in which a polyamide resin or a polyester resin is kneaded with a yellowing inhibitor (A) and an oxidation accelerator (B) in step 1, and then mixed with the polyamide resin (Y).
In the masterbatch method, in step 1, a small amount of polyamide resin or polyester resin is kneaded with the yellowing inhibitor (A) and the oxidation accelerator (B) to form a masterbatch, and then mixed with the remaining polyamide resin (Y). How to do it. Further, when obtaining a masterbatch, the greening inhibitor (C) can also be kneaded at the same time. That is, in step 1, it is preferable to knead the polyamide resin or polyester resin with the yellowing inhibitor (A) and the oxidation accelerator (B) and then mix them with the polyamide resin (Y). In step 1, the polyamide resin or It is more preferable to knead the polyester resin, the yellowing inhibitor (A), the oxidation accelerator (B) and the greening inhibitor (C), and then mix them with the polyamide resin (Y).
A polyamide resin or a polyester resin is preferably used for the master batch, a polyamide resin is preferably used from the viewpoint of compatibility with the polyamide resin (Y), and a polyester resin is used from the viewpoint of suppressing yellowing due to thermal history. It is preferable to use it. In addition, these may be mixed and used.
In particular, the yellowing inhibitor (A) is more preferably a master batch kneaded with a polyamide resin (a master batch containing a polyamide resin and the yellowing inhibitor (A), a polyamide resin composition), and an oxidation accelerator. (B) is more preferably a master batch kneaded with a polyester resin (a master batch containing a polyester resin and an oxidation accelerator (B), a polyester resin composition). The greening inhibitor (C) is a masterbatch kneaded with a polyamide resin (a polyamide resin, a masterbatch containing a yellowing inhibitor (A) and a greening inhibitor (C), a polyamide resin composition). Is preferable.
The polyamide resin used in the masterbatch is preferably a polyamide resin (Y), and more preferably the same as the remaining polyamide resin (Y).
The polyester resin used in the masterbatch is preferably polyester resin (Z). Further, the same material as the polyester resin (X) may be used, or the same material as the polyester resin (X) of the polyester layer may be used.
The amount of the polyamide resin or polyester resin used in the masterbatch is preferably 1 to 20% by mass, more preferably 3 to 15% by mass, based on the amount of the resin in the entire polyamide layer.

When the polyamide resin or polyester resin is kneaded with the yellowing inhibitor (A) and the oxidation accelerator (B) as a method for obtaining a masterbatch, the kneading temperature (° C.) is assumed to be Tm when the melting point of the resin used for the masterbatch is Tm. Is preferably Tm + 5 to Tm + 60, more preferably Tm + 10 to Tm + 50, and even more preferably Tm + 15 to Tm + 40 from the viewpoint of sufficient mixing. Specifically, 245 to 300 ° C. is even more preferable, 250 to 290 ° C. is even more preferable, and 255 to 280 ° C. is even more preferable. The kneading time is preferably 10 to 600 seconds, more preferably 20 to 400 seconds, and even more preferably 30 to 300 seconds from the viewpoint of sufficient mixing. Examples of the device used for kneading include an open type mixing roll, a non-open type Banbury mixer, a kneader, and a continuous kneader (single-screw kneader, twin-screw kneader, multi-screw kneader, etc.).

Examples of the method of mixing the masterbatch with the remaining polyamide resin (Y) include dry blending and further kneading, but dry blending is preferable from the viewpoint of reducing the heat history. For dry blending, it is preferable to mix the pellets of the masterbatch and the pellets of the remaining polyamide resin (Y) with a mixing device such as a tumbler mixer.
When the polyamide layer of the obtained multilayer container contains the polyester resin (Z), the method of mixing the masterbatch with the remaining polyamide resin (Y) and the remaining polyester resin (Z) includes dry blending and further kneading. However, a dry blend is preferable. For the dry blend, it is preferable to mix the pellets of the masterbatch, the pellets of the remaining polyamide resin (Y) and the pellets of the remaining polyester resin (Z) with a mixing device such as a tumbler mixer.

The full compound method is a method of kneading and mixing the entire amount of the polyamide resin (Y) used for the polyamide layer with the yellowing inhibitor (A) and the oxidation accelerator (B).
When the polyamide layer of the obtained multilayer container contains the polyester resin (Z), the total amount of the polyamide resin (Y) used for the polyamide layer, the total amount of the polyester resin (Z), the yellowing inhibitor (A), and the oxidation promotion The agent (B) is kneaded and mixed.
The kneading temperature is preferably 245 to 300 ° C, more preferably 250 to 290 ° C, and even more preferably 255 to 280 ° C from the viewpoint of sufficient mixing. The kneading time is preferably 10 to 600 seconds, more preferably 20 to 400 seconds, and even more preferably 30 to 300 seconds from the viewpoint of sufficient mixing. Examples of the device used for kneading include an open type mixing roll, a non-open type Banbury mixer, a kneader, and a continuous kneader (single-screw kneader, twin-screw kneader, multi-screw kneader, etc.).
The composition of the polyamide resin mixture obtained in this step is preferably the same as that of the <polyamide layer>.

<Step 2 (step to obtain multi-layer preform)>
In step 2, the polyamide resin mixture and the polyester resin composition containing the polyester resin (X) are co-injection molded to obtain a multilayer preform.
The polyester resin composition preferably has the same composition as the <polyester layer>.
In co-injection molding, a mixture of polyester resin and polyamide resin is extruded into a mold and co-injection molded to form a multilayer preform.

<Process 3 (blow molding process)>
In step 3, the multilayer preform is blow-molded.
In the method for producing a multi-layer container of the present invention, it is preferable to mold the multi-layer preform (multi-layer parison) obtained in step 2 by stretching blow.
Among these, in step 2, the multi-layer preform obtained by co-injection molding is preferably stretch-blow molded, and the multi-layer preform obtained by co-injection molding is more preferably biaxially stretch-blow molded. The conditions for biaxial stretch blow molding are that the preform heating temperature is 95 to 110 ° C., the primary blow pressure is 0.5 to 1.2 MPa, and the secondary blow pressure is 2.0 to 2.6 MPa. Preferably, this suppresses the occurrence of uneven thickness and uneven stretching, and a multilayer container having excellent strength can be obtained.

[Manufacturing method of recycled polyester]
The multi-layer container of the present invention is suitable for recycling as described above, and recycled polyester can be produced from the multi-layer container of the present invention as a raw material.
The method for producing recycled polyester of the present invention preferably includes a step of recovering the polyester from the multilayer container.
That is, it has a polyester layer containing a polyester resin (X) and a polyamide layer containing a polyamide resin (Y), a yellowing inhibitor (A) and an oxidation accelerator (B), and the content of the polyamide resin (Y). However, it is 0.05 to 7.0% by mass with respect to the total amount of the total polyamide layer and the total polyester layer, the yellowing inhibitor (A) is a dye, and the content of the yellowing inhibitor (A). However, it is preferable to have a step of recovering the polyester from the multilayer container, which is 1 to 30 ppm with respect to the total amount of the total polyamide layer and the total polyester layer.
The method for producing recycled polyester from a multilayer container is to remove all or part of the polyamide layer from the multilayer container, recover the polyester constituting the polyester layer, and use the polyester as the recycled polyester. Is preferable. The method for producing the recycled polyester from the multilayer container is not limited to the above method, and may be a method for producing the recycled polyester without going through the step of removing the polyamide resin.
The recycled polyester obtained by this production method can be used for various purposes such as resin molded bodies and fibers.
Hereinafter, the method for producing the recycled polyester of the present invention will be described in detail.

In the present manufacturing method, a used multi-layer container is usually used, but an unused container may be used. Examples of the used multi-layer container include those collected once distributed in the market.
In the present manufacturing method, first, when the lid is attached to the multi-layer container, it is preferable to remove the lid from the multi-layer container.
Next, the container is crushed, washed if necessary, separated to selectively take out polyester as needed, and recovered as recycled polyester (recovery step).
Next, if necessary, granulation is performed to obtain pellets (granulation step).
Further, if necessary, a crystallization step and a solid phase polymerization step are performed (crystallization / solid phase polymerization step).
Each process will be described below.

<Recovery process>
The recovery step is a step of crushing the multilayer container to recover the recycled polyester.
Above all, it is preferable to selectively take out the polyester by removing all or a part of the polyamide layer after crushing the multilayer container, and it is more preferable to separate the polyester and the polyamide resin constituting the polyamide layer.
The multi-layer container can be crushed by using a crusher such as a single-screw crusher, a twin-screw crusher, a triaxial crusher, or a cutter mill. The pulverized product obtained by pulverization is, for example, flaky, powdery, or lumpy. However, since most of the multi-layer container has a thin multi-layer laminated structure having a thickness of several mm or less, such as a body portion, most of the crushed material is usually flake-shaped. The flake-shaped crushed product means a flaky or flat product having a thickness of about 2 mm or less.

Further, in the multilayer container, the polyester layer and the polyamide layer are structurally integrated, but usually they are not adhered to each other, and in the pulverization step, the polyester and the polyamide resin are treated as separate pulverized products. Easy to separate. Further, by forming the flakes, it becomes easy to wind up and separate by the air flow of the wind selection separation described later.
However, the polyester and the polyamide resin are not always completely separable in the pulverization step, and the pulverized product has a relatively high polyester content and a relatively low polyester content, so that the polyamide It is separated into those with a relatively high resin content. In the following, for convenience of explanation, a polyester having a relatively high content of polyester is simply referred to as a polyester, and a resin having a relatively high content of a polyamide resin is simply referred to as a polyamide resin.

As described above, the crushed crushed product is separated into polyester and polyamide resin (separation step).
As the sorting method, it is preferable to use specific gravity sorting utilizing the difference in specific densities of polyester and polyamide resin.
That is, it is preferable to remove the polyamide layer by pulverizing the multilayer container and then performing wind selection separation.
Specific examples of the specific gravity sorting include wind sorting separation in which crushed matter is sorted by wind power. The wind selection separation is performed, for example, in a separation device capable of generating a rotating air flow inside, and among the crushed materials applied to the air flow generated by the separation device, the specific gravity is large or the specific surface area is small and the specific surface area is small and the natural weight is used. There is a method of separating and collecting the one that falls and the one that has a small specific gravity or a large specific surface area and is wound up by an air flow.
In this method, the crushed polyester is naturally dropped by its own weight, while the crushed polyamide resin is rolled up, which makes it possible to separate and recover the polyester and the polyamide resin.
In such wind selection separation, the same operation may be repeated for the same pulverized product. For example, the one that has fallen naturally may be further separated by wind selection to increase the polyester content in the recycled polyester.
The sorting method is not limited to wind-selection separation, but is a method of immersing the crushed material in a liquid such as water and separating the crushed material according to the difference in the specific gravity of the crushed material with respect to the liquid. There is a method of separating and separating the water.

<Granulation process>
The recovered recycled polyester is preferably granulated into pellets in order to facilitate handling during molding and the like.
The granulation may be performed before or after the crystallization / solid phase polymerization step described later, but it is better to perform the granulation before the crystallization / solid phase polymerization step. By performing this before the crystallization / solid phase polymerization step, the handleability in the crystallization / solid phase polymerization step is also improved.
In the granulation step, it is preferable to plasticize the pulverized product by melt blending to granulate. Examples of the granulation apparatus for plasticizing and granulating include a single-screw extruder, a twin-screw extruder, a multi-screw extruder, and the like, but any known device can be used. .. The shape of the pellet is preferably cylindrical, spherical, or elliptical spherical.
For granulation, for example, it is preferable to extrude the plasticized recycled polyester into a strand shape and cut it with a pelletizer while cooling it in a water tank to pelletize it. Pellets removed from the aquarium are usually dried to remove moisture adhering to the surface.

<Crystallization / solid phase polymerization process>
After the step of recovering the polyester, it is preferable to carry out one or more steps selected from the crystallization step and the solid phase polymerization step, and it is more preferable to carry out both the crystallization step and the solid phase polymerization step. The crystallization / solid phase polymerization step is preferably performed on the pelletized polyester described above, but may be performed on a non-pelletized polyester (for example, a pulverized product).
When both crystallization and solid-phase polymerization are performed, it is preferable to carry out solid-phase polymerization after crystallization of the polyester.
Crystallization of polyester is carried out by holding the polyester under constant heating. Crystallization is preferably carried out by heating the polyester at, for example, 100 to 230 ° C. By crystallizing the polyester, it is possible to prevent the polyesters from fusing to each other or adhering to the inner surface of the apparatus during solid phase polymerization or molding.

The solid phase polymerization is preferably carried out by keeping the temperature above (melting point of polyester −80 ° C.) or lower and lower than the melting point of polyester for a certain period of time. By setting it below the melting point, it is possible to prevent the polyester from melting, and for example, it is possible to prevent the polyester from adhering to the surface of the apparatus and reducing the work efficiency. Further, when the temperature is set to (melting point −80 ° C.) or higher, the polymerization proceeds at a sufficient polymerization rate and the desired physical properties can be easily obtained.

The solid phase polymerization may be carried out under vacuum or under an inert gas stream such as nitrogen or argon. When carried out under vacuum, 1.0 torr or less is preferable, 0.5 torr or less is more preferable, and 0.1 torr or less is further preferable. Further, it is preferable to reduce the oxygen concentration remaining in the system as much as possible under either vacuum or under an inert gas stream such as nitrogen or argon, and the oxygen concentration is preferably 300 ppm or less, more preferably 30 ppm or less. When the oxygen concentration is 30 ppm or less, appearance defects such as yellowing are less likely to occur.
When the solid phase polymerization is carried out under vacuum, it is preferable to keep the heat transfer uniform while constantly repeating stirring or mixing of the polyester. When carried out in the presence of an inert gas, it is preferable that the surface of the polyester is always kept in contact with the dry gas under a dry gas stream.

The solid phase polymerization equipment for performing the crystallization / solid phase polymerization step is a tumbler type batch type equipment equipped with a heating jacket, a dry silo type equipped with an inert gas airflow facility, a stirring blade and a discharge screw inside. Examples thereof include a crystallization device and a reactor provided with the above. It is preferable that crystallization and solid phase polymerization are continuously or simultaneously performed in the same apparatus.
The heating time for solid-phase polymerization is determined in a timely manner in consideration of the apparatus and other conditions, but it may be any time as long as the polyester can obtain sufficient physical properties.
Since the solid phase polymerization keeps the polyester at a high temperature for a long time, the presence of impurities in the polyester may deteriorate the quality such as color tone. It is preferable that most of the polyamide resin is removed in the removal step described above, and in this case, the deterioration of quality that may occur during solid phase polymerization is minimized.

In the method for producing a recycled polyester of the present invention, a step other than the steps described above may be carried out, or a washing step may be carried out in order to remove the contents adhering to the inside of the multilayer container. The washing is preferably rinsed with a liquid, and washing with water, washing with an alkaline aqueous solution, or both may be performed.
Further, the washing may be performed before the multilayer container is pulverized into pulverized products or after pulverization, but it is better to perform the cleaning before any of granulation, crystallization and solid phase polymerization is performed. preferable. Further, the cleaning step may be performed at the same time as the crushing step by a crusher called a wet crusher that simultaneously performs cleaning and crushing.
Further, when the cleaning step is performed, the drying step may be performed after the cleaning step. By performing the drying step, the water content of the regenerated polyester obtained by this method can be reduced, so that it is possible to provide a high quality regenerated polyester having high thermal stability and the like. The drying step can be performed by using, for example, blowing air with a dryer, hot air, or the like.

When the method for producing the recycled polyester includes a step of removing the polyamide resin, the content of the polyamide resin in the obtained recycled polyester is preferably less than 1% by mass, more preferably less than 0.8% by mass. , More preferably less than 0.6% by mass. By reducing the content of the polyamide resin in this way, the quality of the recycled polyester becomes good.

Hereinafter, the present invention will be described in more detail with reference to Examples and Comparative Examples, but the present invention is not limited to these Examples.

[material]
The polyester resin, yellowing inhibitor, oxidation accelerator and greening inhibitor used in Examples and Comparative Examples are as follows. Further, as the polyamide resin, the one produced in Production Example 1 below was used.
<Polyester resin (X1)>
Isophthalic acid copolymerized polyethylene terephthalate (intrinsic viscosity: 0.83 dL / g, melting point: 248 ° C.), trade name: BK2180, manufactured by Mitsubishi Chemical Corporation <yellowing inhibitor>
Blue RR: Solvent Blue 97 (anthraquinone dye), trade name: MACROLLEX Blue RR Gran, LANXESS K6907: Pigment Blue 15: 1 (α-type copper phthalocyanine pigment), trade name: HELIOGEN BLUE K6907, SF : Powder <oxidation accelerator>
Cobalt stearate (II): manufactured by Tokyo Chemical Industry Co., Ltd. Cobalt neodecanoate (II): manufactured by Nihon Kagaku Sangyo Co., Ltd. <Greening inhibitor>
Violet 3R: Solvent Violet 36 (anthraquinone dye), trade name: MACROLLEX Violet 3R Gran, LANXESS K4535: Pigment Red 202 (quinacridone pigment), trade name: Cinquasia ＞
Isophthalic acid copolymerized polyethylene terephthalate (intrinsic viscosity: 0.83 dL / g, melting point: 248 ° C.), trade name: BK2180, manufactured by Mitsubishi Chemical Corporation

<Polyamide resin (Y1)>
Production Example 1 (Production of Polyamide Resin (Y1))
15,000 g (102.6 mol) of adipic acid precisely weighed in a reaction vessel with an internal volume of 50 liters equipped with a stirrer, a splitter, a total crimp, a thermometer, a dropping funnel, a nitrogen introduction tube, and a strand die. Sodium hypophosphate monohydrate (NaH ₂ PO ₂ · H ₂ O) 13.06 g (123.3 mmol, phosphorus atom concentration in polyamide 151 ppm), sodium acetate 6.849 g (83.49 mmol, hypophosphorus) 0.68) was added as the ratio of the number of moles to sodium monohydrate of acid, and after sufficient nitrogen substitution, the inside of the system was heated to 170 ° C. while stirring under a small amount of nitrogen stream. To this, 13,896 g (102.0 mol, charged molar ratio: 0.994) of metaxylylenediamine was added dropwise under stirring, and the temperature inside the system was continuously raised while removing the generated condensed water from the system. After the dropping of m-xylylenediamine was completed, the reaction was continued for 40 minutes at an internal temperature of 260 ° C. Then, the inside of the system was pressurized with nitrogen, and the polymer was taken out from the strand die and pelletized to obtain about 24 kg of polyamide.
Next, the polyamide was charged in a tumble dryer with a jacket equipped with a nitrogen gas introduction pipe, a vacuum line, a vacuum pump, and a thermocouple for measuring the internal temperature, and while rotating at a constant speed, the purity inside the tumble dryer was 99% by volume. After sufficient replacement with the above nitrogen gas, the tumble dryer was heated under the same nitrogen gas stream, and the pellet temperature was raised to 150 ° C. over about 150 minutes. When the pellet temperature reached 150 ° C., the pressure in the system was reduced to 1 torr or less. The temperature was further increased, the pellet temperature was raised to 200 ° C. over about 70 minutes, and then maintained at 200 ° C. for 30 to 45 minutes. Next, a nitrogen gas having a purity of 99% by volume or more was introduced into the system, and the tumble dryer was cooled while rotating to obtain a polyamide resin (Y1).

[evaluation]
The multilayer container of the present invention was evaluated by the following method.
<Oxygen permeability (evaluation of oxygen barrier property)>
The oxygen permeability was evaluated by the following method.
An oxygen permeability test by the MOCON method was performed according to ASTM D3985. OX-TRAN2 / 61 manufactured by MOCON was used for the measurement. The 500 mL bottles obtained in each Example and Comparative Example were filled with 100 mL of water, and the temperature was 23 ° C., the internal humidity of the bottle was 100% RH, and the external humidity was 50% RH under the condition of an oxygen partial pressure of 0.21 atm. 1 atm of nitrogen was circulated inside the bottle at 20 mL / min, and the inside of the bottle was measured by detecting oxygen contained in the circulated nitrogen with a coulometric sensor. The lower limit of measurement was 0.001 cc / (bottle, day, 0.21 atm).
Judgment was made based on the oxygen permeation amount 7 days after the start of measurement. The smaller the oxygen permeation value, the better the oxygen barrier property.

<Yellowness Δb ^* (evaluation of yellowing inhibitory ability)>
The yellowness Δb ^* of the recycled polyester pellets obtained in [Manufacturing of recycled polyester] described later was measured by the following method and evaluated according to the following criteria.
The color tone of the pellets is based on JIS Z 8722, using a color difference meter ZE-2000 (12V 20W halogen lamp light source manufactured by Nippon Denshoku Kogyo Co., Ltd.), the pellets are fully poured into a 30 mmφ cell container, and measured four times by the reflection method. It was measured as an average value.
The b ^* value represents the chromaticity. + B ^* indicates the yellow direction, and -b ^* indicates the blue direction. Further, the smaller the absolute value of the Δb ^* value, the more the yellowing is suppressed. It also means that the degree of colorlessness is high. The Δb ^* value indicates the difference between the b ^* value of the samples of the following Examples and Comparative Examples and the b ^* value of the polyester resin alone subjected to the same treatment as in the Examples and Comparative Examples.

<Greenness Δa ^* >
The greenness Δa ^* of the recycled polyester pellets obtained in [Manufacturing of recycled polyester] described later was measured by the following method and evaluated according to the following criteria.
The color tone of the pellets is based on JIS Z 8722, using a color difference meter ZE-2000 (12V 20W halogen lamp light source manufactured by Nippon Denshoku Kogyo Co., Ltd.), the pellets are fully poured into a 30 mmφ cell container, and measured four times by the reflection method. It was measured as the average value.
The a ^* value represents the chromaticity. + A ^* indicates the red direction, and -a ^* indicates the green direction. Further, the smaller the absolute value of the Δa ^* value, the more the greening is suppressed. It also means that the degree of colorlessness is high. The Δa ^* value indicates the difference between the a ^* value of the samples of the following Examples and Comparative Examples and the a ^* value of the polyester resin alone subjected to the same treatment as in the Examples and Comparative Examples.

[Manufacturing of polyamide resin mixture by masterbatch method]
Manufacturing example 2
Polyamide resin (Y1) 95.35% by mass, BlueRR 0.20% by mass as a yellowing inhibitor, 4.25% by mass of cobalt stearate (II) as an oxidation accelerator, and Violet3R 0.20% by mass as a greening inhibitor. % Was dry-blended in advance. Next, this dry blend mixture was melt-kneaded at 260 ° C. using a twin-screw extruder (manufactured by Toshiba Machine Co., Ltd., TEM26SX) to obtain masterbatch pellets. Then, the pellet was dried in a vacuum dryer at 150 ° C. for 5 hours to obtain Masterbatch A.
Next, the obtained masterbatch A and the remaining polyamide resin (Y1) were mixed at the mass ratio shown in Table 1 (masterbatch A / remaining polyamide resin = 10/90) to prepare a polyamide resin mixture.

Production example 3
Polyamide resin (Y1) 94.95% by mass, BlueRR 0.40% by mass as a yellowing inhibitor, 4.25% by mass of cobalt stearate (II) as an oxidation accelerator, and Violet3R 0.40% by mass as a greening inhibitor. % Was dry-blended in advance. Next, this dry blend mixture was melt-kneaded at 260 ° C. using a twin-screw extruder (manufactured by Toshiba Machine Co., Ltd., TEM26SX) to obtain masterbatch pellets. Then, the pellet was dried in a vacuum dryer at 150 ° C. for 5 hours to obtain Masterbatch B.
Next, the obtained master batch B and the remaining polyamide resin (Y1) were mixed at the mass ratio shown in Table 1 (master batch B / remaining polyamide resin = 10/90) to prepare a polyamide resin mixture.

Production example 4
Polyamide resin (Y1) 96.48% by mass, BlueRR 0.40% by mass as a yellowing inhibitor, 2.72% by mass of cobalt (II) neodecanoate as an oxidation accelerator, and Violet3R 0.40% by mass as a greening inhibitor. % Was dry-blended in advance. Next, this dry blend mixture was melt-kneaded at 260 ° C. using a twin-screw extruder (manufactured by Toshiba Machine Co., Ltd., TEM26SX) to obtain masterbatch pellets. Then, the pellet was dried in a vacuum dryer at 150 ° C. for 5 hours to obtain Masterbatch C.
Next, the obtained master batch C and the remaining polyamide resin (Y1) were mixed at the mass ratio shown in Table 1 (master batch C / remaining polyamide resin = 10/90) to prepare a polyamide resin mixture.

Production Example 5
Polyamide resin (Y1) 97.08% by mass, BlueRR 0.40% by mass as a yellowing inhibitor, 2.12% by mass of cobalt stearate (II) as an oxidation accelerator, and Violet3R 0.40% by mass as a greening inhibitor. % Was dry-blended in advance. Next, this dry blend mixture was melt-kneaded at 260 ° C. using a twin-screw extruder (manufactured by Toshiba Machine Co., Ltd., TEM26SX) to obtain masterbatch pellets. Then, the pellet was dried in a vacuum dryer at 150 ° C. for 5 hours to obtain Masterbatch D.
Next, the obtained masterbatch D and the remaining polyamide resin (Y1) were mixed at the mass ratio shown in Table 1 (masterbatch D / remaining polyamide resin = 10/90) to prepare a polyamide resin mixture.

Production Example 6
Polyamide resin (Y1) 95.35% by mass, BlueRR 0.40% by mass as a yellowing inhibitor, and cobalt (II) 4.25% by mass as an oxidation accelerator were dry-blended in advance. No greening inhibitor was added to this dry blend. Next, this dry blend mixture was melt-kneaded at 260 ° C. using a twin-screw extruder (manufactured by Toshiba Machine Co., Ltd., TEM26SX) to obtain masterbatch pellets. Then, the pellet was dried in a vacuum dryer at 150 ° C. for 5 hours to obtain Masterbatch E.
Next, the obtained masterbatch E and the remaining polyamide resin (Y1) were mixed at the mass ratio shown in Table 1 (masterbatch E / remaining polyamide resin = 10/90) to prepare a polyamide resin mixture.

Production example 7
Polyester resin (X1) 94.95% by mass, BlueRR 0.40% by mass as a yellowing inhibitor, 4.25% by mass of cobalt stearate (II) as an oxidation accelerator, and Violet3R 0.40% by mass as a greening inhibitor. % Was dry-blended in advance. Next, this dry blend mixture was melt-kneaded at 260 ° C. using a twin-screw extruder (manufactured by Toshiba Machine Co., Ltd., TEM26SX) to obtain masterbatch pellets. Then, the pellet was dried in a vacuum dryer at 150 ° C. for 5 hours to obtain a master batch F.
Next, the obtained master batch F and the remaining polyamide resin (Y1) were mixed at the mass ratio shown in Table 1 (master batch F / remaining polyamide resin = 10/90) to prepare a polyamide resin mixture.

Production Example 8
Polyamide resin (Y1) 93.75% by mass, K6907 0.40% by mass as a yellowing inhibitor, 4.25% by mass of cobalt stearate (II) as an oxidation accelerator, and a pigment as a greening inhibitor. A certain K4535 1.60% by mass was pre-dry blended. Next, this dry blend mixture was melt-kneaded at 260 ° C. using a twin-screw extruder (manufactured by Toshiba Machine Co., Ltd., TEM26SX) to obtain masterbatch pellets. Then, the pellet was dried in a vacuum dryer at 150 ° C. for 5 hours to obtain a master batch G.
Next, the obtained masterbatch G and the remaining polyamide resin (Y1) were mixed at the mass ratio shown in Table 1 (masterbatch G / remaining polyamide resin = 10/90) to prepare a polyamide resin mixture.

Production Example 9
95.75% by mass of the polyamide resin (Y1) and 4.25% by mass of cobalt stearate (II) as an oxidation accelerator were dry-blended in advance. Next, this dry blend mixture was melt-kneaded at 260 ° C. using a twin-screw extruder (manufactured by Toshiba Machine Co., Ltd., TEM26SX) to obtain masterbatch pellets. Then, the pellet was dried in a vacuum dryer at 150 ° C. for 5 hours to obtain Masterbatch H.
Next, the obtained masterbatch H and the remaining polyamide resin (Y1) were mixed at the mass ratio shown in Table 1 (masterbatch H / remaining polyamide resin = 10/90) to prepare a polyamide resin mixture.

[Manufacturing of polyamide resin mixture containing polyester resin]
Production Example 10 (Polyamide resin composition (Y2))
Polyamide resin (Y1) 99.2% by mass, BlueRR 0.4% by mass as a yellowing inhibitor, and Violet3R 0.4% by mass as a greening inhibitor were dry-blended in advance. Next, this dry blend mixture was melt-kneaded at 260 ° C. using a twin-screw extruder (manufactured by Toshiba Machine Co., Ltd., TEM26SX) to obtain masterbatch pellets. Then, the pellet was dried in a vacuum dryer at 150 ° C. for 5 hours to obtain a polyamide resin composition (Y2).

Production Example 11 (Polyester resin composition (Z2))
95.75% by mass of polyester resin (Z1) and 4.25% by mass of cobalt stearate (II) as an oxidation accelerator were dry-blended in advance. Next, this dry blend mixture was melt-kneaded at 280 ° C. using a twin-screw extruder (manufactured by Toshiba Machine Co., Ltd., TEM26SX) to obtain masterbatch pellets. Then, the pellet was dried in a vacuum dryer at 150 ° C. for 5 hours to obtain a polyester resin composition (Z2).

Production Examples 12 to 18 (Polyamide resin mixture containing polyester resin)
The polyamide resin (Y1), the polyamide resin composition (Y2), the polyester resin (Z1) and the polyester resin composition (Z2) were mixed at the mass ratios shown in Table 2 to prepare a polyamide resin mixture. In Table 2, each polyamide resin mixture is indicated by a production example number.

[Manufacturing of multi-layer containers]
Examples 1 to 13 and Comparative Examples 1 to 4
<Preform molding>
Using an injection molding machine with two injection cylinders (manufactured by Sumitomo Heavy Industries, Ltd., model DU130CI) and a two-piece mold (manufactured by Kortec), polyester resin (X1) from one injection cylinder. The polyamide resin mixture obtained in Production Examples 2 to 18 was injected from the other injection cylinder, and under the conditions shown below, a three-layer preform composed of a polyester layer / polyamide layer / polyester layer (preform 1). (A setting equivalent to 25 g per piece) was manufactured by injection molding so that the mass of the polyamide layer with respect to the entire preform was the amount shown in Tables 1 and 2. The shape of the preform was a total length of 95 mm, an outer diameter of 22 mm, and a wall thickness of 4.0 mm. The three-layer preform molding conditions are as shown below.
Skin side injection cylinder temperature: 285 ° C
Core side injection cylinder temperature (3 layers only): 265 ° C
Resin flow path temperature in the mold: 285 ° C
Mold cooling water temperature: 15 ° C
Cycle time: 40 seconds

<Bottle molding>
The preform obtained above was blow-molded by a biaxial stretching blow molding device (EFB1000ET, manufactured by Frontier) to obtain a bottle (hollow multilayer container). The total length of the bottle is 223 mm, the outer diameter is 65 mm, the inner volume is 500 mL, and the bottom is petaloid-shaped. No dimples were provided on the body. The biaxial stretch blow molding conditions are as shown below.
The oxygen permeability was evaluated using the bottles obtained in Examples 1 to 7 and Comparative Examples 1 and 2. The results are shown in Table 1.
Preform heating temperature: 103 ° C
Pressure for stretching rod: 0.7MPa
Primary blow pressure: 1.1 MPa
Secondary blow pressure: 2.5 MPa
Primary blow delay time: 0.30 seconds Primary blow time: 0.30 seconds Secondary blow time: 2.0 seconds Blow exhaust time: 0.6 seconds Mold temperature: 30 ° C

[Manufacturing of recycled polyester]
<Recovery / granulation process>
10 kg of the hollow multilayer containers obtained in Examples 1 to 13 and Comparative Examples 1 to 4 were crushed by a crusher having a mesh diameter of 8 mm, and the obtained flake-shaped crushed products were recovered as recycled polyester.
The recovered recycled polyester is extruded with a twin-screw extruder (manufactured by Toshiba Machine Co., Ltd., TEM26SX) at a heater temperature of 270 ° C. and a discharge rate of 20 kg / hour to form a strand, which is then cut with a pelletizer while being cooled in a water tank. And pelletized. In Examples 1 to 13 and Comparative Examples 1 to 4, the polyamide layer was not separated by wind selection.

<Crystallization / solid phase polymerization process>
The pellets obtained in the granulation step were heated at 200 ° C. for 7 hours under a vacuum reduced to 1 torr or less. The pellets after the heat treatment were taken out and evaluated for yellowness Δb ^* and greenness Δa ^* . The results are shown in Tables 1 and 2.

As shown in Table 1, the multilayer container of the example has an excellent oxygen barrier property, and the yellowing of the regenerated polyester at the time of recycling can be suppressed even by using a small amount of the yellowing inhibitor.

As shown in Table 2, even when the polyamide layer contains a polyester resin, the multilayer container of the example can suppress the yellowing of the recycled polyester at the time of recycling even by using a small amount of the yellowing inhibitor.

[Manufacturing of polyamide resin mixture or polyester resin mixture]
Production Example 19 (Production of Polyamide Resin Mixture)
Polyamide resin (Y1) 94.95% by mass, BlueRR 0.40% by mass as a yellowing inhibitor, 4.25% by mass of cobalt stearate (II) as an oxidation accelerator, and Violet3R 0.40% by mass as a greening inhibitor. % Was dry-blended in advance. Next, this dry blend mixture was melt-kneaded at 260 ° C. using a twin-screw extruder (manufactured by Toshiba Machine Co., Ltd., TEM26SX) to obtain masterbatch pellets. Then, the pellet was dried in a vacuum dryer at 150 ° C. for 5 hours to obtain Masterbatch I.
Next, the obtained masterbatch I and the remaining polyamide resin (Y1) were mixed at the mass ratio shown in Table 3 (masterbatch I / remaining polyamide resin = 10/90) to prepare a polyamide resin mixture.

Production Example 20 (Production of Polyamide Resin Mixture)
95.75% by mass of the polyamide resin (Y1) and 4.25% by mass of cobalt stearate (II) as an oxidation accelerator were dry-blended in advance. Next, this dry blend mixture was melt-kneaded at 260 ° C. using a twin-screw extruder (manufactured by Toshiba Machine Co., Ltd., TEM26SX) to obtain masterbatch pellets. Then, the pellet was dried in a vacuum dryer at 150 ° C. for 5 hours to obtain a master batch J.
Next, the obtained masterbatch J and the remaining polyamide resin (Y1) were mixed at the mass ratio shown in Table 3 (masterbatch J / remaining polyamide resin = 10/90) to prepare a polyamide resin mixture.

Production Example 21 (Production of polyester resin mixture)
97.60% by mass of polyester resin (X1), 1.20% by mass of BlueRR as a yellowing inhibitor, and 1.20% by mass of Violet3R as a greening inhibitor were dry-blended in advance. Next, this dry blend mixture was melt-kneaded at 260 ° C. using a twin-screw extruder (manufactured by Toshiba Machine Co., Ltd., TEM26SX) to obtain masterbatch pellets. Then, the pellet was dried in a vacuum dryer at 150 ° C. for 5 hours to obtain Masterbatch K.
Next, the obtained masterbatch K and the remaining polyester resin (X1) were mixed at the mass ratio shown in Table 3 (masterbatch K / remaining polyester resin = 5/95) to prepare a polyester resin mixture.

[Manufacturing of multi-layer containers]
Example 14 and Comparative Example 5
<Preform molding>
Using an injection molding machine with two injection cylinders (manufactured by Sumitomo Heavy Industries, Ltd., model DU130CI) and a two-piece mold (manufactured by Kortec), polyester resin (X1) from one injection cylinder. (Example 14) or the polyester resin mixture (Comparative Example 5) obtained in Production Example 21 is obtained from the other injection cylinder in the polyamide resin mixture (Example 14) or Production Example 20 obtained in Production Example 19. By injecting the obtained polyamide resin mixture (Comparative Example 5), a three-layer preform composed of a polyester layer / polyamide layer / polyester layer (setting equivalent to 25 g per preform) is formed under the conditions shown below. It was manufactured by injection molding so that the mass of the polyamide layer with respect to the entire preform was the amount shown in Table 3. The shape of the preform was a total length of 95 mm, an outer diameter of 22 mm, and a wall thickness of 4.0 mm. The three-layer preform molding conditions are as shown below.
Skin side injection cylinder temperature: 285 ° C
Core side injection cylinder temperature (3 layers only): 265 ° C
Resin flow path temperature in the mold: 285 ° C
Mold cooling water temperature: 15 ° C
Cycle time: 40 seconds

<Bottle molding>
The preform obtained above was blow-molded by a biaxial stretching blow molding device (EFB1000ET, manufactured by Frontier) to obtain a bottle (hollow multilayer container). The total length of the bottle is 223 mm, the outer diameter is 65 mm, the inner volume is 500 mL, and the bottom is petaloid-shaped. No dimples were provided on the body. The biaxial stretch blow molding conditions are as shown below.
Preform heating temperature: 103 ° C
Pressure for stretching rod: 0.7MPa
Primary blow pressure: 1.1 MPa
Secondary blow pressure: 2.5 MPa
Primary blow delay time: 0.30 seconds Primary blow time: 0.30 seconds Secondary blow time: 2.0 seconds Blow exhaust time: 0.6 seconds Mold temperature: 30 ° C

[Manufacturing of recycled polyester including wind sorting process]
<Collection / Wind selection / Granulation process>
10 kg of the hollow multilayer container obtained in Example 14 and Comparative Example 5 was pulverized with a crusher having a mesh diameter of 8 mm to form flakes, and then the flakes were washed with water. Then, using a floss separator CFS-150 (manufactured by Accor Co., Ltd.), the material that had a heavy specific gravity and fell into the underlay was recovered at a supply speed of 10 kg / hr, a suction blower of 35 Hz, and a secondary blower of 30 Hz. Finally, the flake-shaped crushed material that fell into the underlay was recovered as recycled polyester.
The recovered recycled polyester is extruded with a twin-screw extruder (manufactured by Toshiba Machine Co., Ltd., TEM26SX) at a heater temperature of 270 ° C. and a discharge rate of 20 kg / hour to form a strand, which is then cut with a pelletizer while being cooled in a water tank. And pelletized.

<Crystallization / solid phase polymerization process>
The pellets obtained in the granulation step were heated at 200 ° C. for 7 hours under a vacuum reduced to 1 torr or less. The pellets after the heat treatment were taken out and evaluated for yellowness Δb ^* and greenness Δa ^* . The results are shown in Table 3.

As shown in Table 3, the multilayer container of Example 14 can suppress the yellowing of the recycled polyester even when the polyamide layer is removed during recycling by adding a small amount of the yellowing inhibitor to the polyamide layer. rice field. In the multilayer container of Comparative Example 5, when the polyamide layer was removed at the time of recycling by adding the yellowing inhibitor to the polyester layer, the quantitative balance between the polyamide resin contained in the recycled polyester and the yellowing inhibitor was balanced. It collapsed and the Δb ^* value became large.

Claims (23)

A polyester layer containing a polyester resin (X) and
It has a polyamide layer containing a polyamide resin (Y), a yellowing inhibitor (A), and an oxidation accelerator (B).
The content of the polyamide resin (Y) is 0.05 to 7.0% by mass with respect to the total amount of all the polyamide layers and all polyester layers.
The yellowing inhibitor (A) is an anthraquinone dye,
A multi-layer container in which the content of the yellowing inhibitor (A) is 1 to 30 ppm with respect to the total amount of all the polyamide layers and all polyester layers. A constituent unit derived from a dicarboxylic acid in which the polyester resin (X) contains 80 mol% or more of a constituent unit derived from terephthalic acid, and a constituent unit derived from a diol containing 80 mol% or more of a constituent unit derived from ethylene glycol. The multilayer container according to claim 1, further comprising. The composition of the polyamide resin (Y) derived from a diamine containing 80 mol% or more of a constituent unit derived from xylylenediamine and a dicarboxylic acid containing 80 mol% or more of a constituent unit derived from adipic acid. The multilayer container according to claim 1 or 2, having a unit. The multilayer container according to any one of claims 1 to 3, wherein the oxidation accelerator (B) is a compound containing a transition metal. The multilayer container according to claim 4, wherein the transition metal is at least one selected from the group consisting of cobalt, iron, manganese, and nickel. The multilayer container according to any one of claims 1 to 5 , wherein the polyamide layer further contains a greening inhibitor (C). The multilayer container according to claim 6 , wherein the greening inhibitor (C) is at least one selected from the group consisting of anthraquinone dyes and azo dyes. The multilayer container according to any one of claims 1 to 7 , wherein the polyamide layer further contains a polyester resin (Z). The multilayer container according to claim 8 , wherein the content of the polyester resin (Z) in the polyamide layer is 5 to 70% by mass. The multi-layer container according to any one of claims 1 to 9 , wherein the multi-layer container is a multi-layer hollow container. The multi-layer container according to any one of claims 1 to 10 , wherein the multi-layer container has a 2- to 5-layer structure and the outermost layer is a polyester layer. The multi-layer container according to any one of claims 1 to 11 , wherein the multi-layer container has a 3 to 5 layer structure, and the outermost layer and the innermost layer are polyester layers. A polyester layer containing a polyester resin (X) and
It has a polyamide layer containing a polyamide resin (Y), a yellowing inhibitor (A), and an oxidation accelerator (B).
The content of the polyamide resin (Y) is 0.05 to 7.0% by mass with respect to the total amount of all the polyamide layers and all polyester layers.
The yellowing inhibitor (A) is an anthraquinone dye,
A method for producing a multilayer container in which the content of the yellowing inhibitor (A) is 1 to 30 ppm with respect to the total amount of all the polyamide layers and all polyester layers.
Step 1, to prepare a polyamide resin mixture by mixing a polyamide resin (Y), a yellowing inhibitor (A), and an oxidation accelerator (B).
Production of a multi-layer container including the step 2 of co-injection molding the polyamide resin mixture and the polyester resin composition containing the polyester resin (X) to obtain a multi-layer preform, and the step 3 of blow-molding the multi-layer preform. Method. The method for producing a multilayer container according to claim 13 , wherein in step 1, the greening inhibitor (C) is further mixed. The method for producing a multilayer container according to claim 13 or 14 , wherein the polyester resin (Z) is further mixed in step 1. The invention according to any one of claims 13 to 15 , wherein in step 1, the polyamide resin or polyester resin, the yellowing inhibitor (A) and the oxidation accelerator (B) are kneaded and then mixed with the polyamide resin (Y). How to make a multilayer container. The method for producing a multilayer container according to any one of claims 13 to 16 , wherein the oxidation accelerator (B) is a compound containing a transition metal. The method for manufacturing a multilayer container according to claim 17 , wherein the transition metal is at least one selected from the group consisting of cobalt, iron, manganese, and nickel. The method for producing a multilayer container according to any one of claims 14 to 18 , wherein the greening inhibitor (C) is at least one selected from the group consisting of anthraquinone dyes and azo dyes. A method for producing recycled polyester, which comprises a step of recovering polyester from the multilayer container according to any one of claims 1 to 12 . The method for producing a recycled polyester according to claim 20 , further comprising a step of removing all or a part of the polyamide layer from the multilayer container to recover the polyester. The method for producing a recycled polyester according to claim 20 or 21 , wherein the polyamide layer is removed by crushing the multilayer container and then performing wind selection separation. The method for producing a recycled polyester according to any one of claims 20 to 22 , wherein one or more steps selected from a crystallization step and a solid phase polymerization step are performed after the step of recovering the polyester.