JP2001162678A - Method for producing multi-layer container - Google Patents

Method for producing multi-layer container

Info

Publication number
JP2001162678A
JP2001162678A JP34996099A JP34996099A JP2001162678A JP 2001162678 A JP2001162678 A JP 2001162678A JP 34996099 A JP34996099 A JP 34996099A JP 34996099 A JP34996099 A JP 34996099A JP 2001162678 A JP2001162678 A JP 2001162678A
Authority
JP
Japan
Prior art keywords
layer
ethylene
thermoplastic resin
container
resin layer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP34996099A
Other languages
Japanese (ja)
Inventor
Shigeki Takada
重喜 高田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kuraray Co Ltd
Original Assignee
Kuraray Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kuraray Co Ltd filed Critical Kuraray Co Ltd
Priority to JP34996099A priority Critical patent/JP2001162678A/en
Publication of JP2001162678A publication Critical patent/JP2001162678A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain a multi-layer container which has good gas-barrier properties and can be recovered/recycled with a thermoplastic resin layer separated from a barrier layer after being used. SOLUTION: In a method for producing the multi-layer container, a multi- layer sheet obtained by dry-laminating a water-soluble ethylene-modified polyvinyl alcohol resin layer 1-19 mole % in ethylene-modification degree and a thermoplastic resin layer is thermoformed.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、熱可塑性樹脂層と
水溶性のエチレン変性ポリビニルアルコール系樹脂層を
ドライラミネートして得た多層シートを熱成形する容器
の製造方法に関する。さらに詳しくは、ガスバリヤー性
を有し、かつ使用後、熱可塑性樹脂層とバリヤー層を分
離し、回収、再利用が可能な容器の製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing a container for thermoforming a multilayer sheet obtained by dry laminating a thermoplastic resin layer and a water-soluble ethylene-modified polyvinyl alcohol-based resin layer. More particularly, the present invention relates to a method for producing a container having gas barrier properties and capable of separating a thermoplastic resin layer and a barrier layer after use, and recovering and reusing the container.

【0002】[0002]

【従来の技術】近年、食料品や飲料、医薬品等の容器と
して熱可塑性樹脂製の容器が多く用いられている。例え
ば、ポリプロピレンやポリエステル樹脂、ポリスチレン
樹脂等の熱可塑性樹脂のシートを真空成形、圧空成形、
プレス成形して製造されるカップ等が挙げられる。該熱
可塑性樹脂製容器は軽量性、加工性、取り扱い容易性等
から各種用途に多用されている。
2. Description of the Related Art In recent years, thermoplastic resin containers have been widely used as containers for foodstuffs, beverages, pharmaceuticals and the like. For example, a sheet of a thermoplastic resin such as polypropylene, polyester resin, and polystyrene resin is vacuum formed, pressure-formed,
Examples include a cup manufactured by press molding. The thermoplastic resin container is frequently used for various purposes because of its light weight, workability, ease of handling, and the like.

【0003】しかしながら、ガスバリヤー性が必要とさ
れる用途、例えば食料品用カップ等の容器では、このよ
うにして得られた熱可塑性樹脂製成形物ではガスバリヤ
ー性が不十分である場合が多い。その改善策として該熱
可塑性樹脂層にガスバリヤー性に優れたエチレン−酢酸
ビニル共重合体けん化物(以下EVOHと略記する)層
を積層することが試みられている。すなわち、熱可塑性
樹脂層/EVOH層/熱可塑性樹脂層等のように3種以
上の積層構造を有する成形物の検討がなされている。例
えば、熱可塑性樹脂層/EVOH層/熱可塑性樹脂層の
3層構造を有するシートを成形する方法が用いられてい
る。
However, in applications where gas barrier properties are required, for example, containers such as food cups, the thermoplastic resin molded products obtained in this way often have insufficient gas barrier properties. . As an improvement measure, an attempt has been made to laminate a saponified ethylene-vinyl acetate copolymer (hereinafter abbreviated as EVOH) layer having excellent gas barrier properties on the thermoplastic resin layer. That is, a molded article having three or more types of laminated structures such as a thermoplastic resin layer / EVOH layer / thermoplastic resin layer has been studied. For example, a method of forming a sheet having a three-layer structure of a thermoplastic resin layer / EVOH layer / thermoplastic resin layer has been used.

【0004】しかしながら、市販のEVOHはエチレン
変性度が20モル%を超えているため水に不溶であり、
EVOH層を有する容器は、使用された後、熱可塑性樹
脂とEVOH層の分離が容易ではなく、容器の再利用が
困難であるという問題があり、使用後、熱可塑性樹脂層
とバリヤー層を分離し、回収、再利用が可能な容器が望
まれていた。
However, commercially available EVOH is insoluble in water because the degree of ethylene modification exceeds 20 mol%.
A container having an EVOH layer has a problem that, after being used, it is difficult to separate the thermoplastic resin and the EVOH layer, and it is difficult to reuse the container. After use, the thermoplastic resin layer and the barrier layer are separated. A container that can be collected and reused has been desired.

【0005】[0005]

【発明が解決しようとする課題】本発明の目的は、ガス
バリヤー性を有し、かつ使用後、熱可塑性樹脂層とバリ
ヤー層を分離し、回収、再利用が可能な容器を提供する
ことにある。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a container having a gas barrier property and capable of separating a thermoplastic resin layer and a barrier layer after use, and recovering and reusing the container. is there.

【0006】[0006]

【課題を解決するための手段】上記目的は、エチレン変
性度が1〜19モル%でかつ水溶性のエチレン変性ポリ
ビニルアルコール系樹脂(以下エチレン変性PVAと略
記することがある)層と熱可塑性樹脂層をドライラミネ
ートして得た多層シートを熱成形する多層容器の製造方
法を提供することによって達成される。
An object of the present invention is to provide a water-soluble ethylene-modified polyvinyl alcohol resin (hereinafter sometimes abbreviated as ethylene-modified PVA) layer having a degree of ethylene modification of 1 to 19 mol% and a thermoplastic resin. This is achieved by providing a method for producing a multilayer container for thermoforming a multilayer sheet obtained by dry laminating layers.

【0007】[0007]

【発明の実施の形態】以下に本発明についてさらに詳細
に説明する。本発明に使用される熱可塑性樹脂は、熱溶
融可能で、かつ耐水性を有するものであれば特に限定は
なく、種々の熱可塑性樹脂が使用可能であるが、ポリエ
チレンテレフタレート(PET)、ポリプロピレン(P
P)、ポリエチレン(PE)、ポリスチレン(PS)、
ポリアミド(PA)等が好適に用いられる。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in more detail. The thermoplastic resin used in the present invention is not particularly limited as long as it is heat-fusible and has water resistance, and various thermoplastic resins can be used, and polyethylene terephthalate (PET), polypropylene ( P
P), polyethylene (PE), polystyrene (PS),
Polyamide (PA) or the like is preferably used.

【0008】本発明に使用されるエチレン変性PVA系
樹脂とは、ビニルエステルとエチレンを常法により共重
合した後、けん化して得られる水溶性の重合体である。
ここでビニルエステルとは酢酸ビニル、プロピオン酸ビ
ニル、ギ酸ビニル、バーサチック酸ビニル、ピバリン酸
ビニルなどが挙げられるが、工業的に生産されコスト的
に有利な酢酸ビニルが通常使用される。また得られる変
性PVAが水溶性であれば、他の単量体、たとえばα−
オレフィン、ω−ヒドロキシ−α−オレフィン、不飽和
カルボン酸塩、長鎖ビニルエーテル、ポリオキシアルキ
レン基含有不飽和化合物、飽和分岐脂肪酸ビニル、不飽
和スルホン酸塩、シラノール基含有不飽和化合物、アミ
ノ基含有不飽和化合物等で変性されていてもよい。エチ
レンの変性度は、1〜19モル%であることが重要であ
り、好ましくは3モル%以上、更に好ましくは5モル%
以上、最適には7モル%以上であり、また上限について
は好ましくは18モル%以下、更に好ましくは15モル
%以下、最適には13モル%以下である。エチレン変性
度が1モル%より低いと、特に高湿度下で充分なガスバ
リヤー性を発現することができなくなる。一方エチレン
変性度が19モル%を超えると水溶性が著しく低下し、
使用後容器の、熱可塑性樹脂層とバリヤー層の分離、回
収、再利用が困難となる。
The ethylene-modified PVA resin used in the present invention is a water-soluble polymer obtained by copolymerizing a vinyl ester and ethylene by a conventional method and then saponifying the copolymer.
Here, the vinyl ester includes vinyl acetate, vinyl propionate, vinyl formate, vinyl versatate, vinyl pivalate, and the like. Vinyl acetate that is industrially produced and has a cost advantage is usually used. If the resulting modified PVA is water-soluble, other monomers such as α-
Olefin, ω-hydroxy-α-olefin, unsaturated carboxylate, long-chain vinyl ether, unsaturated compound containing polyoxyalkylene group, saturated branched fatty acid vinyl, unsaturated sulfonate, unsaturated compound containing silanol group, containing amino group It may be modified with an unsaturated compound or the like. It is important that the degree of modification of ethylene is 1 to 19 mol%, preferably 3 mol% or more, more preferably 5 mol%.
As described above, it is optimally at least 7 mol%, and the upper limit is preferably at most 18 mol%, more preferably at most 15 mol%, optimally at most 13 mol%. If the degree of ethylene modification is lower than 1 mol%, sufficient gas barrier properties cannot be exhibited, particularly under high humidity. On the other hand, if the degree of ethylene modification exceeds 19 mol%, the water solubility significantly decreases,
It becomes difficult to separate, collect, and reuse the thermoplastic resin layer and the barrier layer of the container after use.

【0009】本発明に用いられるエチレン変性PVAの
けん化度は、80モル%以上であることが好ましく、9
0モル%以上であることがより好ましく、95モル%以
上であることが特に好ましい。けん化度が80モル%よ
り低いと、得られた容器のバリヤー性が著しく低下す
る。
The degree of saponification of the ethylene-modified PVA used in the present invention is preferably 80 mol% or more.
It is more preferably at least 0 mol%, particularly preferably at least 95 mol%. If the degree of saponification is lower than 80 mol%, the barrier properties of the obtained container are significantly reduced.

【0010】本発明に用いられるエチレン変性PVA系
樹脂の重合度は、JIS K6726にて測定した粘度
平均重合度(以下単に重合度略記する)で200〜50
00であることが好ましく、300〜3000であるこ
とがより好ましい。重合度が200未満では、得られた
容器に落下等の衝撃を加えた時にエチレン変性PVA系
樹脂層が割れたり、外観を損ねたりする恐れがある。一
方重合度が5000を超えると、エチレン変性PVA系
樹脂の粘度が著しく高くなり、熱溶融成形が困難とな
る。
The degree of polymerization of the ethylene-modified PVA resin used in the present invention is 200 to 50 as a viscosity average degree of polymerization (hereinafter simply referred to as degree of polymerization) measured according to JIS K6726.
00, more preferably 300 to 3000. If the degree of polymerization is less than 200, the ethylene-modified PVA-based resin layer may be broken or its appearance may be damaged when an impact such as dropping is applied to the obtained container. On the other hand, when the degree of polymerization exceeds 5,000, the viscosity of the ethylene-modified PVA-based resin becomes extremely high, so that hot melt molding becomes difficult.

【0011】本発明に用いられるエチレン変性PVA系
樹脂は水溶性であることが必要である。ここで水溶性と
は、エチレン変性PVA系樹脂に水を加え、1〜80w
t%のいずれかの濃度にしたとき、95℃の温度で、固
形物が認められず、かつ均一な溶液になることを指す。
ここで言う均一とは必ずしも透明である必要はない。
The ethylene-modified PVA resin used in the present invention must be water-soluble. Here, the term "water-soluble" means that water is added to an ethylene-modified PVA resin,
It means that at a temperature of 95 ° C., no solid matter is observed and a homogeneous solution is obtained at any concentration of t%.
Here, “uniform” does not necessarily have to be transparent.

【0012】本発明に用いるエチレン変性PVA系樹脂
には、本発明の目的を損なわない範囲で、必要に応じて
種々の添加剤を適宜配合することができる。添加剤の例
として、可塑剤、酸化防止剤、加工安定剤、紫外線吸収
剤、着色剤、香料、滑剤、剥離剤、帯電防止剤、補強
剤、増量剤、フィラー等公知の添加剤が挙げられる。特
にモンモリロナイト等の板状クレー、膨潤性合成雲母等
は好適に用いられる。
The ethylene-modified PVA-based resin used in the present invention may contain various additives, if necessary, as long as the object of the present invention is not impaired. Examples of additives include known additives such as plasticizers, antioxidants, processing stabilizers, ultraviolet absorbers, coloring agents, fragrances, lubricants, release agents, antistatic agents, reinforcing agents, extenders, and fillers. . Particularly, plate-like clay such as montmorillonite, swellable synthetic mica, and the like are preferably used.

【0013】本発明に用いる多層シートとは、上記のエ
チレン変性PVA系樹脂を1層または2層以上有し、か
つ熱可塑性樹脂層を1層または2層以上有する多層シー
トである。多層シートは、ドライラミネートにより得る
ことが重要であり、ラミネート方法としては、エチレン
変性PVA系樹脂と熱可塑性樹脂を加圧ラミネートする
方法等が一般的である。ドライラミネートする事によ
り、熱可塑性樹脂層とバリアー層であるエチレン変性P
VA系樹脂層の分離、回収が良好となり、またバリアー
層の湿度依存性も少なくなる。ラミネートして多層シー
トを得る場合、熱可塑性樹脂層とエチレン変性PVA系
樹脂層の間には熱可塑性樹脂とエチレン変性PVAとの
接着性が良好となるよう接着層を設けることができる。
接着層に用いられる接着剤は、多層シートを構成する熱
可塑性樹脂層とエチレン変性PVA系樹脂層との接着性
を向上させるものであれば特に限定はなく、公知の接着
剤が使用できる。また、エチレン変性PVA系樹脂層が
多層シートの中間層であることが望ましい。即ち、熱可
塑性樹脂層/エチレン変性PVA系樹脂層/熱可塑性樹
脂層のように、中間層のエチレン変性PVA層の両側層
に熱可塑性樹脂層を設けた多層シートが好適である。多
層容器の最外層を熱可塑性樹脂層にする場合、得られた
多層容器は表面の耐水性、取り扱い性等が向上する。
The multilayer sheet used in the present invention is a multilayer sheet having one or two or more layers of the above-mentioned ethylene-modified PVA resin and one or two or more thermoplastic resin layers. It is important that the multilayer sheet is obtained by dry lamination, and as a lamination method, a method of laminating an ethylene-modified PVA-based resin and a thermoplastic resin under pressure and the like is general. By dry laminating, the thermoplastic resin layer and the barrier layer, ethylene-modified P
The separation and recovery of the VA-based resin layer is improved, and the humidity dependence of the barrier layer is reduced. When a multilayer sheet is obtained by laminating, an adhesive layer can be provided between the thermoplastic resin layer and the ethylene-modified PVA-based resin layer so that the adhesion between the thermoplastic resin and the ethylene-modified PVA becomes good.
The adhesive used for the adhesive layer is not particularly limited as long as it improves the adhesiveness between the thermoplastic resin layer constituting the multilayer sheet and the ethylene-modified PVA-based resin layer, and a known adhesive can be used. Further, it is desirable that the ethylene-modified PVA-based resin layer is an intermediate layer of the multilayer sheet. That is, a multilayer sheet in which thermoplastic resin layers are provided on both sides of an intermediate ethylene-modified PVA layer, such as a thermoplastic resin layer / ethylene-modified PVA-based resin layer / thermoplastic resin layer, is preferable. When the outermost layer of the multilayer container is a thermoplastic resin layer, the resulting multilayer container has improved surface water resistance, handleability, and the like.

【0014】多層シートの厚みは、通常10〜5000
μmのものが用いられ、50〜3000μmのものが好
ましく、100〜2000μmのものが特に好ましい。
エチレン変性PVA系樹脂層の厚みは所望のガスバリヤ
ー性に応じて適宜設定できるが、通常1〜1000μm
であり、3〜500μmであることが好ましい。接着剤
層の厚みは、通常1〜500μmであり、3〜300μ
mであることが好ましく、5〜100μmであることが
更に好ましい。
The thickness of the multilayer sheet is usually 10 to 5000
μm is used, preferably 50 to 3000 μm, and particularly preferably 100 to 2000 μm.
The thickness of the ethylene-modified PVA-based resin layer can be appropriately set according to the desired gas barrier properties, but is usually 1 to 1000 μm.
And preferably from 3 to 500 μm. The thickness of the adhesive layer is usually 1 to 500 μm, and 3 to 300 μm.
m, more preferably 5 to 100 μm.

【0015】本発明の多層容器は、上記多層シートを熱
成形して得られる。熱成形方法に特に限定はないが、通
常真空成形、圧空成形、プレス成形等で成形される。こ
こで成形前または成形の際に、多層シートの少なくとも
一部を1.2倍以上、好ましくは2.0倍以上に延伸す
ることが望ましい。ここで延伸とは多層シートを構成す
る熱可塑性樹脂のガラス転移点温度以上かつ融点以下の
温度で引き延ばすことを指し、一方向に延伸してもよ
く、二方向以上に延伸しても良い。延伸倍率は、もとの
多層シート厚みを、成形後の容器厚みで除した数値で示
される。延伸により、得られた容器のガスバリヤー性、
耐水性及び透明性が向上する。
The multilayer container of the present invention is obtained by thermoforming the above-mentioned multilayer sheet. The thermoforming method is not particularly limited, but is usually formed by vacuum forming, pressure forming, press forming or the like. Here, it is desirable that at least a part of the multilayer sheet is stretched 1.2 times or more, preferably 2.0 times or more before or during the forming. Here, the term “stretching” refers to stretching at a temperature not lower than the glass transition temperature and not higher than the melting point of the thermoplastic resin constituting the multilayer sheet, and may be stretched in one direction or in two or more directions. The stretching ratio is indicated by a value obtained by dividing the thickness of the original multilayer sheet by the thickness of the container after molding. By stretching, the gas barrier properties of the obtained container,
Water resistance and transparency are improved.

【0016】かかる方法で得られた本発明の多層容器
は、ガスバリヤー性に優れており、食料品、飲料、調味
料や医薬品の容器等に幅広く利用できる。またバリヤー
層であるエチレン変性PVA系樹脂が水溶性であるた
め、熱水や水蒸気等で熱可塑性樹脂と分離でき、容器の
回収、再利用が可能である。
The multilayer container of the present invention obtained by such a method has excellent gas barrier properties and can be widely used for containers of foodstuffs, beverages, seasonings and pharmaceuticals. Further, since the ethylene-modified PVA-based resin as the barrier layer is water-soluble, it can be separated from the thermoplastic resin with hot water or steam, and the container can be collected and reused.

【0017】[0017]

【実施例】以下に実施例を挙げて本発明をさらに詳しく
説明するが、本発明はこれによって限定されるものでは
ない。なお、実施例中特に断りのないかぎり「%」およ
び「部」は重量基準を表す。また特性値の測定方法及び
評価方法は次の方法による。
EXAMPLES The present invention will be described in more detail with reference to the following Examples, but it should not be construed that the present invention is limited thereto. In the examples, “%” and “parts” are based on weight unless otherwise specified. The method for measuring and evaluating the characteristic value is as follows.

【0018】(1)特性値の測定方法 (1−1)重合度、けん化度 JIS K6726にて測定した。(1) Method of measuring characteristic values (1-1) Degree of polymerization and degree of saponification Measured according to JIS K6726.

【0019】(2)評価方法 (2−1)ガスバリヤー性 容器に味噌を満杯になるまで充填し、乾燥窒素で十分パ
ージ後密封した。30℃、65%RHの恒温恒湿槽に3
0日間放置後の中身の味噌の変色度合いからガスバリヤ
ー性を評価した。評価結果は次の表示により示す。 ◎:極めて良好(全く変色無し) ○:良好(ほとんど変色無し) △:やや不良(わずかに変色した) ×:不良(かなり変色した)
(2) Evaluation method (2-1) Gas barrier property A container was filled with miso until it was full, and the container was purged with dry nitrogen and sealed. 30 ° C, 65% RH in a constant temperature and humidity chamber
The gas barrier property was evaluated from the degree of discoloration of the miso after standing for 0 days. The evaluation result is shown by the following display. ◎: extremely good (no discoloration) ○: good (no discoloration) △: slightly poor (slightly discolored) ×: bad (very discolored)

【0020】(2−2)耐水性 容器の表面に水1mlを滴下し、指でこすって表面の溶
出程度から耐水性を評価した。評価結果は次の表示によ
り示す。 ◎:極めて良好(全く溶出無し) ○:良好(ほとんど溶出無し) △:やや不良(わずかに溶出した) ×:不良(かなり溶出した)
(2-2) Water resistance 1 ml of water was dropped on the surface of the container and rubbed with a finger to evaluate the water resistance from the degree of elution of the surface. The evaluation result is shown by the following display. ◎: extremely good (no elution at all) ○: good (almost no elution) △: slightly poor (slightly eluted) ×: poor (very eluted)

【0021】(2−3)回収性 多層容器を粉砕し、95℃の熱水に2時間浸漬し、熱可
塑性樹脂層とバリヤー層との分離程度を評価した。評価
結果は次の表示により示す。 ◎:極めて良好(バリヤー層が完全に溶出しており、分
離極めて容易) ○:良好(バリヤー層が若干未溶出であるが、分離容
易) △:やや不良(バリヤー層がほとんど未溶出であり、分
離やや困難) ×:不良(バリヤー層が全く未溶出であり、分離不可
能)
(2-3) Recoverability The multilayer container was pulverized and immersed in hot water at 95 ° C. for 2 hours to evaluate the degree of separation between the thermoplastic resin layer and the barrier layer. The evaluation result is shown by the following display. :: Very good (barrier layer is completely eluted and very easy to separate) ○: Good (barrier layer is slightly eluted but easy to separate) △: Slightly poor (barrier layer is hardly eluted and ×: poor (barrier layer is not eluted at all and cannot be separated)

【0022】実施例1 粘度平均重合度1000、エチレン変性度7モル%、け
ん化度98.0モル%のエチレン変性PVA15wt%含
む水溶液を、先端に巾600mmのTダイを有する50
mmφ単軸押出機(プラスチック工学研究所製)より押
出し、乾燥することで厚さ50μmのキャストフィルム
を作製した。またポリエチレンテレフタレート(以下P
ETと略記)を同様にTダイを有する押出機を用い、2
80℃で溶融押出成形して厚さ200μmのフィルムを
作製した。PETフィルムにドライラミネーション接着
剤としてタケラックA−385(主剤)/タケネートA
−10(硬化剤)を酢酸エチルを希釈剤としてドライラ
ミネーターにて固形分3g/m2塗布し、これに先に作
製したエチレン変性PVAフィルムをPET/接着剤/
エチレン変性PVA/接着剤/PETの構成になるよう
ドライラミネートして厚さ470μmの3種5層のシー
トを得た。得られた3種5層のシートを130℃に加熱
後、圧空成形し、12cm×12cm×高さ7cmのカ
ップ状容器を得た。容器の延伸倍率及びガスバリヤー
性、耐水性、回収性を測定した。結果を表1に示す。
Example 1 An aqueous solution containing 15% by weight of ethylene-modified PVA having a viscosity-average degree of polymerization of 1,000, a degree of ethylene modification of 7 mol%, and a degree of saponification of 98.0 mol% has a T-die having a width of 600 mm at its tip.
It was extruded from a mmφ single screw extruder (manufactured by Plastics Engineering Laboratory) and dried to produce a cast film having a thickness of 50 μm. In addition, polyethylene terephthalate (hereinafter P
(Abbreviated as ET) in the same manner using an extruder having a T die.
The film was melt-extruded at 80 ° C. to produce a film having a thickness of 200 μm. Takelac A-385 (base) / takenate A as dry lamination adhesive on PET film
-10 (curing agent) was applied with a solid content of 3 g / m 2 using a dry laminator using ethyl acetate as a diluent, and the ethylene-modified PVA film prepared earlier was subjected to PET / adhesive /
Dry lamination was performed so as to have a configuration of ethylene-modified PVA / adhesive / PET to obtain a sheet of three types and five layers having a thickness of 470 μm. The resulting three-layer, five-layer sheet was heated to 130 ° C., and then subjected to pressure forming to obtain a cup-shaped container having a size of 12 cm × 12 cm × 7 cm. The stretch ratio, gas barrier properties, water resistance, and recoverability of the container were measured. Table 1 shows the results.

【0023】実施例2〜5 変性PVAのエチレン変性度、けん化度が異なる以外
は、実施例1と同様にカップ状容器を得た。結果を表1
に示す。
Examples 2 to 5 A cup-shaped container was obtained in the same manner as in Example 1 except that the modified PVA had different degrees of ethylene modification and saponification. Table 1 shows the results
Shown in

【0024】実施例6〜7 圧空成形における延伸倍率が異なる以外は実施例1と同
様にカップ状容器を得た。結果を表1に示す。
Examples 6 and 7 Cup-shaped containers were obtained in the same manner as in Example 1 except that the stretching ratio in the pressure forming was different. Table 1 shows the results.

【0025】実施例8 3種5層のシートのかわりに、PET/接着剤/エチレ
ン変性PVAの構成になるようドライラミネートして得
られた厚さ260μmの3種3層シート用い、エチレン
変性PVA層が外側にくるよう成形した以外は実施例1
と同様にカップ状容器を得た。結果を表1に示す。
Example 8 Instead of a three-layer, five-layer sheet, a three-layer, 260 μm-thick three-layer sheet obtained by dry lamination to have a structure of PET / adhesive / ethylene-modified PVA was used. Example 1 except that the layer was formed so as to be on the outside
To obtain a cup-shaped container. Table 1 shows the results.

【0026】実施例9 3種5層のシートのかわりに接着剤層を設けていない、
PET/エチレン変性PVA/PETの構成となるよう
ドライラミネートし厚さ450μmの2種3層シートを
用いた以外は実施例1と同様にカップ状容器を得た。結
果を表1に示す。
Example 9 An adhesive layer was not provided in place of the three-layer five-layer sheet.
A cup-shaped container was obtained in the same manner as in Example 1 except that dry lamination was performed so as to have a structure of PET / ethylene-modified PVA / PET, and a 450 μm-thick two-layer three-layer sheet was used. Table 1 shows the results.

【0027】比較例1 エチレン変性PVAのかわりに未変性PVAを用いた以
外は実施例1と同様にカップ状容器を得た。結果を表1
に示す。
Comparative Example 1 A cup-shaped container was obtained in the same manner as in Example 1 except that unmodified PVA was used instead of ethylene-modified PVA. Table 1 shows the results
Shown in

【0028】比較例2 エチレン変性度が0.5モル%である以外は実施例1と
同様にカップ状容器を得た。結果を表1に示す。
Comparative Example 2 A cup-shaped container was obtained in the same manner as in Example 1, except that the degree of ethylene modification was 0.5 mol%. Table 1 shows the results.

【0029】比較例3 エチレン変性度が28モル%である以外は実施例1と同
様にカップ状容器を得た。結果を表1に示す。
Comparative Example 3 A cup-shaped container was obtained in the same manner as in Example 1 except that the degree of ethylene modification was 28 mol%. Table 1 shows the results.

【0030】[0030]

【表1】 [Table 1]

【0031】[0031]

【発明の効果】本発明により得られた多層容器は、ガス
バリヤー性に優れており、食料品(飲料、調味料、アル
コール類等)や医薬品の容器等に幅広く利用できるし、
また使用後、熱可塑性樹脂層とバリヤー層を分離し、回
収、再利用が可能である。
The multilayer container obtained by the present invention has excellent gas barrier properties, and can be widely used for food (drinks, seasonings, alcohols, etc.) and pharmaceutical containers.
Also, after use, the thermoplastic resin layer and the barrier layer can be separated, recovered and reused.

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4F100 AK01B AK01C AK04A AK21A AK42 AL06A BA02 BA03 BA06 BA10B BA10C BA13 CB01 DA01 EC182 EH012 EJ372 GB16 GB23 GB66 JB09A JB16B JB16C JD02 JL16 YY00A 4F208 AA04 AA11 AA13 AA19C AA24 AA29 AC03 AE10 AG03 AG07 AH55 MA02 MB01 MB22 MG01 MG04 MG07 MG12 MG22 ──────────────────────────────────────────────────続 き Continued on the front page F-term (reference) 4F100 AK01B AK01C AK04A AK21A AK42 AL06A BA02 BA03 BA06 BA10B BA10C BA13 CB01 DA01 EC182 EH012 EJ372 GB16 GB23 GB66 JB09A JB16B JB16C JD02 JL16 YY04 A10AA AA AA AA AA AAC A AH55 MA02 MB01 MB22 MG01 MG04 MG07 MG12 MG22

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 エチレン変性度が1〜19モル%でかつ
水溶性のエチレン変性ポリビニルアルコール系樹脂層と
熱可塑性樹脂層をドライラミネートして得た多層シート
を熱成形することを特徴とする多層容器の製造方法。
A multilayer sheet obtained by dry laminating a water-soluble ethylene-modified polyvinyl alcohol-based resin layer and a thermoplastic resin layer having a degree of ethylene modification of 1 to 19 mol% and thermoforming. Container manufacturing method.
【請求項2】 多層シートが、中間層のエチレン変性ポ
リビニルアルコール系樹脂層と該中間層の両側層の熱可
塑性樹脂層をドライラミネートして得た多層シートであ
る請求項1記載の多層容器の製造方法。
2. The multilayer container according to claim 1, wherein the multilayer sheet is a multilayer sheet obtained by dry laminating an ethylene-modified polyvinyl alcohol-based resin layer as an intermediate layer and thermoplastic resin layers on both sides of the intermediate layer. Production method.
【請求項3】 多層シートを、熱成形前または熱成形中
に1.2倍以上に延伸する請求項1または2記載の多層
容器の製造方法。
3. The method for producing a multilayer container according to claim 1, wherein the multilayer sheet is stretched 1.2 times or more before or during thermoforming.
JP34996099A 1999-12-09 1999-12-09 Method for producing multi-layer container Pending JP2001162678A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34996099A JP2001162678A (en) 1999-12-09 1999-12-09 Method for producing multi-layer container

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34996099A JP2001162678A (en) 1999-12-09 1999-12-09 Method for producing multi-layer container

Publications (1)

Publication Number Publication Date
JP2001162678A true JP2001162678A (en) 2001-06-19

Family

ID=18407281

Family Applications (1)

Application Number Title Priority Date Filing Date
JP34996099A Pending JP2001162678A (en) 1999-12-09 1999-12-09 Method for producing multi-layer container

Country Status (1)

Country Link
JP (1) JP2001162678A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003047854A1 (en) * 2001-12-06 2003-06-12 Arrow Coated Products Limited Multilayered films
JP2007290378A (en) * 2006-03-28 2007-11-08 Nippon Synthetic Chem Ind Co Ltd:The Blow molded container
WO2012023779A2 (en) * 2010-08-16 2012-02-23 Skc Co., Ltd. Environmentally friendly multilayer barrier film and preparation method thereof
KR101159158B1 (en) 2010-10-29 2012-06-25 에스케이씨 주식회사 Environmentally friendly multi-layer barrier film and preparation method thereof

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003047854A1 (en) * 2001-12-06 2003-06-12 Arrow Coated Products Limited Multilayered films
JP2007290378A (en) * 2006-03-28 2007-11-08 Nippon Synthetic Chem Ind Co Ltd:The Blow molded container
WO2012023779A2 (en) * 2010-08-16 2012-02-23 Skc Co., Ltd. Environmentally friendly multilayer barrier film and preparation method thereof
WO2012023779A3 (en) * 2010-08-16 2012-05-31 Skc Co., Ltd. Environmentally friendly multilayer barrier film and preparation method thereof
KR101156600B1 (en) * 2010-08-16 2012-06-20 에스케이씨 주식회사 Environmental friendly multi-layer barrier film and preparation method thereof
KR101159158B1 (en) 2010-10-29 2012-06-25 에스케이씨 주식회사 Environmentally friendly multi-layer barrier film and preparation method thereof

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