JPH11198225A - Laminate stretching method - Google Patents

Laminate stretching method

Info

Publication number
JPH11198225A
JPH11198225A JP1330498A JP1330498A JPH11198225A JP H11198225 A JPH11198225 A JP H11198225A JP 1330498 A JP1330498 A JP 1330498A JP 1330498 A JP1330498 A JP 1330498A JP H11198225 A JPH11198225 A JP H11198225A
Authority
JP
Japan
Prior art keywords
stretching
laminate
evoh
layer
vinyl acetate
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
JP1330498A
Other languages
Japanese (ja)
Inventor
Tomoyuki Yamamoto
友之 山本
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.)
Mitsubishi Chemical Corp
Original Assignee
Nippon Synthetic Chemical Industry 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 Nippon Synthetic Chemical Industry Co Ltd filed Critical Nippon Synthetic Chemical Industry Co Ltd
Priority to JP1330498A priority Critical patent/JPH11198225A/en
Publication of JPH11198225A publication Critical patent/JPH11198225A/en
Pending legal-status Critical Current

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  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
  • Laminated Bodies (AREA)
  • Heating, Cooling, Or Curing Plastics Or The Like In General (AREA)

Abstract

PROBLEM TO BE SOLVED: To improve gas barrier properties, transparency, tensile strength and a draw ratio by a laminate consisting of a saponified ethylene-vinyl acetate copolymer layer and a thermoplastic resin layer is drawn while being irradiated with microwaves. SOLUTION: As EVOH of a saponified ethylene-vinyl acetate copolymer EVOH layer, a substance in which an ethylene content is 10-60 mole % and the degree of saponification of a vinyl acetate component is 90 mole %. is used. A polyolefin resin and others are used as the thermoplastic resin of a thermoplastic resin layer. Both layers are coextruded to form a laminate. The laminate is drawn while being irradiated with microwaves. First, the undrawn laminate is drawn longitudinally in the first drawing process and then is drawn crosswise in the second drawing process to obtain a biaxially oriented laminate. Since the EVOH laminate is drawn while being irradiated with microwaves, gas barrier properties, transparency, tensile strength, and others improve.

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、エチレン−酢酸ビ
ニル共重合体ケン化物(以下、EVOHと略記する)層
と熱可塑性樹脂層の積層体の延伸方法に関する。
The present invention relates to a method for stretching a laminate of a saponified ethylene-vinyl acetate copolymer (hereinafter abbreviated as EVOH) layer and a thermoplastic resin layer.

【0002】[0002]

【従来の技術】従来より、EVOHは、そのガスバリヤ
ー性を生かして、各種包装用途に多用されているが、通
常は、各種の熱可塑性樹脂と積層されて、積層体として
実用に供されているのが実情である。そして、かかる積
層体は、積層体強度の向上、引き裂き性の付与、ガスバ
リヤー性の向上等のために、1軸或いは2軸に延伸処理
が施されているのが一般的である。かかる延伸に際して
は、延伸性を上げるために、延伸温度を高くしたり、可
塑剤を添加したりすることが試みられている。
2. Description of the Related Art Heretofore, EVOH has been widely used for various packaging applications by taking advantage of its gas barrier properties. However, usually, EVOH is laminated with various thermoplastic resins and practically used as a laminate. That is the fact. Such a laminate is generally subjected to uniaxial or biaxial stretching in order to improve the strength of the laminate, impart tearability, improve gas barrier properties, and the like. At the time of stretching, attempts have been made to increase the stretching temperature or to add a plasticizer in order to increase the stretchability.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、発明者
の詳細な検討によれば、延伸時に延伸温度を高くし過ぎ
ると積層されているポリオレフィン系樹脂等の熱可塑性
樹脂層が結晶化して透明性が失われ、また、可塑剤等の
添加物を用いると積層体の層間接着力が低下するなどの
悪影響が出ることも多く、可塑剤等の添加物を用いるこ
となく、透明性の低下も起こさず、高延伸が行える延伸
方法が望まれるところである。
However, according to a detailed study by the inventor, if the stretching temperature is too high during stretching, the laminated thermoplastic resin layer such as a polyolefin resin crystallizes and the transparency is lowered. Loss, also, when using an additive such as a plasticizer, often has an adverse effect such as a decrease in the interlayer adhesion of the laminate, without using an additive such as a plasticizer, does not cause a decrease in transparency There is a demand for a stretching method capable of performing high stretching.

【0004】[0004]

【課題を解決するための手段】そこで、本発明者はかか
る事情に鑑みて鋭意研究を重ねた結果、EVOH層と熱
可塑性樹脂層からなる積層体にマイクロ波を照射しなが
ら延伸することにより、ガスバリヤー性は勿論のこと、
透明性、引張強度等に優れた高延伸倍率(1.5〜8
倍)の積層体が得られることを見出し本発明を完成する
に至った。
Accordingly, the present inventor has conducted intensive studies in view of the above circumstances, and as a result, the laminate comprising the EVOH layer and the thermoplastic resin layer is stretched while being irradiated with microwaves. Not to mention gas barrier properties,
High draw ratio (1.5 to 8) excellent in transparency, tensile strength, etc.
The present invention has been found that a laminate of (2) is obtained.

【0005】[0005]

【発明の実施の形態】以下、本発明の延伸方法について
具体的に説明する。本発明に用いられる積層体は、EV
OH層と熱可塑性樹脂層からなるもので、該EVOH層
に用いられるEVOHとしては、特に限定されないが、
エチレン含量10〜60モル%、好ましくは20〜60
モル%、更に好ましくは25〜55モル%、酢酸ビニル
成分のケン化度が90モル%以上、好ましくは95モル
%以上のものが用いられ、エチレン含量が10モル%未
満では耐水性が不十分となり、一方60モル%を越える
とガスバリヤー性が低下して好ましくない。又、ケン化
度が90モル%未満では耐水性が不十分となって好まし
くない。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The stretching method of the present invention will be specifically described below. The laminate used in the present invention is EV
It is composed of an OH layer and a thermoplastic resin layer, and the EVOH used for the EVOH layer is not particularly limited,
Ethylene content 10-60 mol%, preferably 20-60
Mol%, more preferably 25 to 55 mol%, and the saponification degree of the vinyl acetate component is 90 mol% or more, preferably 95 mol% or more. When the ethylene content is less than 10 mol%, the water resistance is insufficient. On the other hand, if it exceeds 60 mol%, the gas barrier property is undesirably lowered. On the other hand, if the saponification degree is less than 90 mol%, the water resistance becomes insufficient, which is not preferable.

【0006】又、該EVOHは必要に応じて、種々変性
されていても良く、又該変性EVOHと上記EVOHの
混合物でも良い。該変性EVOHとしては、例えば、プ
ロピレン、イソブテン等による変性EVOH、炭素数3
〜30のα−オレフィンの少なくとも1種又は炭素数3
〜30のα−オレフィンの少なくとも1種とエチレンに
よる変性EVOH、アクリル酸エステルをグラフト重合
して得られる変性EVOH、(メタ)アクリル酸エステ
ル−エチレン−酢酸ビニルからなる3元共重合体をケン
化して得られる変性EVOH、EVOHの水酸基をシア
ノエチル基により変性した変性EVOH、ポリエステル
をビニルアルコールと解重合反応させてなるポリエステ
ルグラフト物を含有する変性EVOH、酢酸ビニル−エ
チレン−ケイ素含有オレフィン性不飽和単量体の共重合
体をケン化して得られる変性EVOH、ピロリドン環含
有単量体−エチレン−酢酸ビニルからなる3元共重合体
をケン化して得られる変性EVOH、アクリルアミド−
エチレン−酢酸ビニルからなる3元共重合体をケン化し
て得られる変性EVOH、酢酸アリル−エチレン−酢酸
ビニルからなる3元共重合体をケン化して得られる変性
EVOH、酢酸イソプロペニル−エチレン−酢酸ビニル
からなる3元共重合体をケン化して得られる変性EVO
H、ポリエーテル成分がEVOHの末端に付加している
変性EVOH、ポリエーテル成分がEVOHの枝ポリマ
ーとしてグラフト状に付加している変性EVOH、アル
キレンオキサイドがEVOHに付加した変性EVOH等
が挙げられる。本発明で用いられるEVOHには、必要
に応じて、酸化防止剤、滑剤、アンチブロッキング剤、
着色剤、帯電防止剤、紫外線吸収剤等を添加することも
できる。
[0006] The EVOH may be variously modified, if necessary, or may be a mixture of the modified EVOH and the EVOH. As the modified EVOH, for example, modified EVOH with propylene, isobutene, etc., having 3 carbon atoms
At least one α-olefin having from 30 to 30 carbon atoms or 3 carbon atoms
Saponified terpolymer comprising modified EVOH, modified EVOH obtained by graft polymerization of at least one α-olefin of at least 30 and ethylene and acrylic acid ester, and (meth) acrylate-ethylene-vinyl acetate Modified EVOH, a modified EVOH obtained by modifying the hydroxyl group of EVOH with a cyanoethyl group, a modified EVOH containing a polyester graft obtained by depolymerizing a polyester with vinyl alcohol, a vinyl acetate-ethylene-silicon-containing olefinically unsaturated monomer EVOH obtained by saponifying a monomeric copolymer, modified EVOH obtained by saponifying a terpolymer comprising a pyrrolidone ring-ethylene-vinyl acetate, acrylamide-
Modified EVOH obtained by saponifying a terpolymer of ethylene-vinyl acetate, modified EVOH obtained by saponifying a terpolymer of allyl acetate-ethylene-vinyl acetate, isopropenyl acetate-ethylene-acetic acid Modified EVO obtained by saponifying vinyl terpolymer
H, modified EVOH in which a polyether component is added to the terminal of EVOH, modified EVOH in which a polyether component is added in a graft form as a branch polymer of EVOH, and modified EVOH in which an alkylene oxide is added to EVOH. In the EVOH used in the present invention, if necessary, an antioxidant, a lubricant, an anti-blocking agent,
Coloring agents, antistatic agents, ultraviolet absorbers and the like can also be added.

【0007】又、EVOHは上記以外のα−オレフィ
ン、不飽和カルボン酸又はその塩・部分アルキルエステ
ル・完全アルキルエステル・ニトリル・アミド・無水
物、不飽和スルホン酸又はその塩等のコモノマーを含ん
でいても差支えない。また、熱可塑性樹脂層に用いられ
る熱可塑性樹脂としては、直鎖状低密度ポリエチレン、
低密度ポリエチレン、中密度ポリエチレン、高密度ポリ
エチレン、エチレン−酢酸ビニル共重合体、アイオノマ
ー、エチレン−プロピレン共重合体、エチレン−アクリ
ル酸エステル共重合体、ポリプロピレン、プロピレン−
α−オレフィン(炭素数4〜20のα−オレフィン)共
重合体、ポリブテン、ポリペンテン等のオレフィンの単
独又は共重合体、或いはこれらのオレフィンの単独又は
共重合体を不飽和カルボン酸又はそのエステルでグラフ
ト変性したもの等の広義のポリオレフィン系樹脂、ポリ
スチレン系樹脂、ポリエステル、ポリアミド、共重合ポ
リアミド、ポリ塩化ビニル、ポリ塩化ビニリデン、アク
リル系樹脂、ビニルエステル系樹脂、ポリエステルエラ
ストマー、ポリウレタンエラストマー、塩素化ポリエチ
レン、塩素化ポリプロピレン等を挙げることができ、中
でもポリオレフィン系樹脂、ポリアミド系樹脂、ポリエ
ステル系樹脂、ポリスチレン系樹脂が好適に用いられ
る。
EVOH contains comonomer other than the above, such as α-olefins, unsaturated carboxylic acids or salts thereof, partial alkyl esters, complete alkyl esters, nitriles, amides, anhydrides, unsaturated sulfonic acids or salts thereof. You can be there. Further, as the thermoplastic resin used for the thermoplastic resin layer, linear low-density polyethylene,
Low-density polyethylene, medium-density polyethylene, high-density polyethylene, ethylene-vinyl acetate copolymer, ionomer, ethylene-propylene copolymer, ethylene-acrylate copolymer, polypropylene, propylene
α-olefin (α-olefin having 4 to 20 carbon atoms) copolymer, homo- or copolymer of olefin such as polybutene, polypentene, or homo- or copolymer of these olefins with unsaturated carboxylic acid or ester thereof Broadly defined polyolefin resin such as graft-modified resin, polystyrene resin, polyester, polyamide, copolymerized polyamide, polyvinyl chloride, polyvinylidene chloride, acrylic resin, vinyl ester resin, polyester elastomer, polyurethane elastomer, chlorinated polyethylene And chlorinated polypropylene. Among them, a polyolefin resin, a polyamide resin, a polyester resin, and a polystyrene resin are preferably used.

【0008】上記のEVOHと熱可塑性樹脂を用いて、
EVOH層と熱可塑性樹脂層からなる積層体を作製する
に当たっては、公知の方法を採用することができ、例え
ば、EVOH層及び熱可塑性樹脂層を予め作製しておい
て、両者を有機チタン化合物、イソシアネート化合物、
ポリエステル系化合物等の公知の接着剤を用いてラミネ
ートする方法、EVOH及び熱可塑性樹脂を溶融共押出
により積層体とする方法、押出コーティングする方法等
が挙げられる。本発明においては、上記の如き得られた
積層体を延伸するにあたって、マイクロ波を照射しなが
ら、延伸することに最大の特徴を有するもので、かかる
方法について説明する。
Using the above EVOH and thermoplastic resin,
In producing a laminate including an EVOH layer and a thermoplastic resin layer, a known method can be employed.For example, an EVOH layer and a thermoplastic resin layer are produced in advance, and both are formed of an organic titanium compound. Isocyanate compound,
A method of laminating using a known adhesive such as a polyester compound, a method of forming a laminate by melt co-extrusion of EVOH and a thermoplastic resin, and a method of extrusion coating are exemplified. In the present invention, when the obtained laminate is stretched while being irradiated with microwaves, it has the greatest feature in stretching, and such a method will be described.

【0009】本発明において、マイクロ波を照射させる
ためには、例えば、商用周波数が2.45GHzで、電
力0.1〜2kwのマイクロ波発生装置を用いればよ
く、かかるマイクロ波の照射時間としては、1〜300
秒が好ましく、かかる時間が1秒未満では、照射の効果
が期待できず、逆に300秒を越えるとEVOHが加熱
されすぎて延伸配向の向上が期待できない。更に好まし
くは2〜180秒である。尚、延伸については、1軸、
2軸(同時、逐次)、ブロー延伸等のいずれに限定され
るものではないが、ここでは、2軸(逐次)延伸につい
て説明する。
In the present invention, in order to irradiate microwaves, for example, a microwave generator having a commercial frequency of 2.45 GHz and a power of 0.1 to 2 kW may be used. , 1-300
Seconds are preferred. If the time is less than 1 second, the effect of irradiation cannot be expected. If the time exceeds 300 seconds, the EVOH is heated too much and improvement in stretch orientation cannot be expected. More preferably, it is 2 to 180 seconds. For stretching, uniaxial,
Although not limited to any of biaxial (simultaneous and sequential) and blow stretching, biaxial (sequential) stretching will be described here.

【0010】本発明において、マイクロ波照射は、第1
次(MD方向)延伸工程又は第2次(TD方向)延伸工
程のいずれか、或いは両方の工程において行うことがで
きるが、ここでは、両方の工程でマイクロ波照射を行う
場合について説明する。先ず、延伸前の積層体は、第1
次(MD方向)延伸工程に供される。かかる第1次(M
D方向)延伸は、公知の方法を利用することができ、本
発明では、かかる延伸時に該積層体の表面に上記のマイ
クロ波を照射するのであるが、具体的には、延伸装置の
上下(又は左右)に前記の如きマイクロ波発生装置を取
り付ければよい。このときの積層体の温度は、100〜
160℃に調整することも好ましく、かかる温度が10
0℃未満では外層の熱可塑性樹脂を十分に延伸すること
が困難となり、逆に160℃を越えると外層の熱可塑性
樹脂が溶けたり、結晶化を起こして白濁して好ましくな
い。このときの延伸倍率は規定されないが、本発明では
高延伸倍率とすることが可能で、かかる積層体を縦(M
D)方向に1.5〜8倍(更に好ましくは、2〜8倍)
に延伸することが好ましい。
[0010] In the present invention, microwave irradiation is performed in the first step.
The stretching can be performed in either the next (MD direction) stretching step or the second (TD direction) stretching step or in both steps. Here, a case where microwave irradiation is performed in both steps will be described. First, the laminate before stretching is the first
The next (MD direction) stretching step is performed. The first (M
For the stretching in the D direction), a known method can be used. In the present invention, the surface of the laminate is irradiated with the above-described microwave at the time of such stretching. Or the left and right) may be attached with the microwave generator as described above. The temperature of the laminate at this time is 100 to
It is also preferable to adjust the temperature to 160 ° C.
If the temperature is lower than 0 ° C., it is difficult to sufficiently stretch the thermoplastic resin in the outer layer. On the other hand, if the temperature exceeds 160 ° C., the thermoplastic resin in the outer layer melts or crystallizes, which is not preferable. Although the stretching ratio at this time is not specified, in the present invention, a high stretching ratio can be used.
1.5 to 8 times (more preferably 2 to 8 times) in the direction D)
It is preferred that the film be stretched to

【0011】上記の第1次(MD方向)延伸された積層
体は、次いで第2次(TD方向)延伸工程で横方向に延
伸されるのであるが、このときにも第1次(MD方向)
延伸時と同様の方法で行うことができる。このときの延
伸倍率も特に規定されないが、かかる積層体を横(T
D)方向に1.5〜8倍(更に好ましくは、2〜8倍)
に延伸することが好ましい。通常、かかる第2次延伸
は、積層体両耳部をクリップではさむテンター方式で行
われるが、一般的に公知の方法で行ってもよい。また、
通常は更に熱固定を行う。熱固定とは緊張下に120℃
〜積層体の融点より5℃低い温度で数秒ないし数分間積
層体を加熱することである。
The above-mentioned first (MD direction) stretched laminate is then stretched in the transverse direction in the second (TD direction) stretching step. )
The stretching can be performed in the same manner as in the stretching. Although the stretching ratio at this time is not particularly specified, such a laminate is placed horizontally (T
1.5 to 8 times (more preferably 2 to 8 times) in the direction D)
It is preferred that the film be stretched to Usually, such secondary stretching is performed by a tenter method in which both ears of the laminate are sandwiched by clips, but may be performed by a generally known method. Also,
Usually, heat setting is further performed. Heat setting is 120 ° C under tension
Heating the laminate at a temperature 5 ° C. lower than the melting point of the laminate for several seconds to several minutes.

【0012】かくして、2軸延伸積層体が得られるわけ
であるが、1軸延伸の場合も上記に準じて行えばよい。
また、本発明の積層体の層構成としては、EVOH層を
A、熱可塑性樹脂層をBとするとき、A/B以外に、B
/A/B、A/B/A、B/A/B/A、B/A/B/
A/B等の積層体構造とすることも可能である。
In this way, a biaxially stretched laminate is obtained. In the case of uniaxial stretching, it may be performed according to the above.
When the layer structure of the laminate of the present invention is A, the EVOH layer is B, and the thermoplastic resin layer is B.
/ A / B, A / B / A, B / A / B / A, B / A / B /
It is also possible to adopt a laminate structure such as A / B.

【0013】かくして、本発明の延伸方法で得られた
(延伸)積層体は、外観特性、ガスバリヤー性等に優れ
るため、食品や医薬品、農薬品、工業薬品包装用のフィ
ルム、シート、チューブ、袋、容器、レトルト容器等の
用途に非常に有用である。尚、本発明の延伸方法は、E
VOH単層の延伸にも有用な方法でもある。
Thus, the (stretched) laminate obtained by the stretching method of the present invention is excellent in appearance characteristics, gas barrier properties, etc., and therefore, is suitable for packaging films, sheets, tubes, foods, pharmaceuticals, agricultural chemicals and industrial chemicals. It is very useful for applications such as bags, containers, and retort containers. In addition, the stretching method of the present invention uses E
It is also a useful method for stretching a VOH monolayer.

【0014】[0014]

【実施例】以下、実施例を挙げて本発明を具体的に説明
する。尚、例中、「部」、「%」とあるのは、特に断り
のない限り重量基準を意味する。 実施例1 ポリプロピレン[日本ポリケム社製、『ノバテックPP
EG8』]層(100μm厚)/接着樹脂[三井石油
化学社製、『アドマー QF500』]層(30μm)
/EVOH[エチレン含有量32モル%、ケン化度9
9.8モル%]層(30μm厚)/接着樹脂[同上]層
(30μm)/ポリプロピレン[同上]層(100μm
厚)の積層体を下記の条件で逐次2軸延伸及び熱固定を
行って、2軸延伸積層体を得た。
The present invention will be specifically described below with reference to examples. In the examples, “parts” and “%” mean on a weight basis unless otherwise specified. Example 1 Polypropylene [manufactured by Nippon Polychem, "Novatech PP"
EG8]] layer (100 μm thickness) / adhesive resin [Mitsui Petrochemical Co., Ltd., “Admer QF500”] layer (30 μm)
/ EVOH [ethylene content 32 mol%, saponification degree 9
9.8 mol%] layer (30 μm thick) / adhesive resin [same as above] layer (30 μm) / polypropylene [same as above] layer (100 μm
Thickness) was sequentially biaxially stretched and heat-set under the following conditions to obtain a biaxially stretched laminate.

【0015】[第1次延伸(縦延伸)条件] マイクロ波の周波数 2.45GHz マイクロ波発生器の電力 1kw マイクロ波の照射時間 15秒 延伸機 ロール式延伸機 延伸温度 140℃ 縦方向延伸倍率 3.6倍 延伸後の膜厚 75μm [第2次延伸(横延伸)条件] マイクロ波の周波数 同上 マイクロ波発生器の電力 同上 マイクロ波の照射時間 同上 延伸機 テンター式延伸機 延伸温度 140℃ 横方向延伸倍率 3.9倍 延伸後の膜厚 17μm 延伸後のフィルム幅 800mm [熱固定条件] 温度 160℃ 時間 5秒 得られた2軸延伸積層体のガスバリヤー性、透明性、引
張強度について、下記の如く評価を行った。
[Primary stretching (longitudinal stretching) conditions] Microwave frequency 2.45 GHz Power of microwave generator 1 kW Microwave irradiation time 15 seconds Stretcher Roll type stretcher Stretching temperature 140 ° C. Stretching ratio in longitudinal direction 3 .6 times film thickness after stretching 75 μm [Secondary stretching (transverse stretching) conditions] Microwave frequency Same as above Power of microwave generator Same as above Microwave irradiation time Same as above Stretching machine Tenter stretching machine Stretching temperature 140 ° C Lateral direction Stretch ratio 3.9 times Film thickness after stretching 17 μm Film width after stretching 800 mm [Heat setting conditions] Temperature 160 ° C. Time 5 seconds Regarding gas barrier properties, transparency and tensile strength of the obtained biaxially stretched laminate, The evaluation was performed as follows.

【0016】(ガスバリヤー性)20℃、65%RHの
条件下で、酸素透過度(cc/m2・day・atm)
を測定した。 (透明性)ヘイズ値を測定した。 (引張強度の向上性)20℃、65%RHの条件下で、
ASTM−D−882及び同1922に準拠して縦方向
と横方向の引張強度を測定し、別途マイクロ波を照射せ
ずに延伸した(延伸倍率:3×3倍)フィルムの引張強
度を測定して、縦方向及び横方向共にマイクロ波照射し
ながら延伸したフィルムより引張強度が向上が認められ
るかどうかを調べた。
(Gas barrier property) Oxygen permeability (cc / m 2 · day · atm) under conditions of 20 ° C. and 65% RH
Was measured. (Transparency) The haze value was measured. (Improvement of tensile strength) Under the conditions of 20 ° C. and 65% RH,
In accordance with ASTM-D-882 and 1922, the tensile strength in the longitudinal direction and the transverse direction was measured, and the tensile strength of the film stretched without irradiation with microwaves (stretch ratio: 3 × 3 times) was measured. Then, it was examined whether or not the tensile strength was improved from a film stretched while irradiating microwaves in both the longitudinal and transverse directions.

【0017】実施例2 実施例1において、延伸条件を下記の如く変更した以外
は同様に行って、2軸延伸積層体得て、同様に評価を行
った。 [第1次延伸(縦延伸)条件] マイクロ波の周波数 2.45GHz マイクロ波発生器の電力 1.3kw マイクロ波の照射時間 20秒 延伸機 ロール式延伸機 延伸温度 140℃ 縦方向延伸倍率 4.8倍 延伸後の膜厚 60μm [第2次延伸(横延伸)条件] マイクロ波の周波数 同上 マイクロ波発生器の電力 同上 マイクロ波の照射時間 同上 延伸機 テンター式延伸機 延伸温度 140℃ 横方向延伸倍率 5.2倍 延伸後の膜厚 14μm 延伸後のフィルム幅 800mm
Example 2 A biaxially stretched laminate was obtained in the same manner as in Example 1 except that the stretching conditions were changed as described below, and the evaluation was performed in the same manner. [Primary stretching (longitudinal stretching) conditions] Microwave frequency 2.45 GHz Power of microwave generator 1.3 kW Microwave irradiation time 20 seconds Stretching machine Roll stretching machine Stretching temperature 140 ° C Longitudinal stretching magnification 4. Eight times Thickness after stretching 60 μm [Secondary stretching (transverse stretching) conditions] Microwave frequency Same as above Power of microwave generator Same as above Microwave irradiation time Same as above Stretching machine Tenter stretching machine Stretching temperature 140 ° C Lateral stretching Magnification 5.2 times Film thickness after stretching 14 μm Film width after stretching 800 mm

【0018】実施例3 実施例1において、延伸条件を下記の如く変更した以外
は同様に行って、2軸延伸積層体得て、同様に評価を行
った。 [第1次延伸(縦延伸)条件] マイクロ波の周波数 2.45GHz マイクロ波発生器の電力 0.2kw マイクロ波の照射時間 5秒 延伸機 ロール式延伸機 延伸温度 150℃ 縦方向延伸倍率 3.5倍 延伸後の膜厚 80μm [第2次延伸(横延伸)条件] マイクロ波の周波数 同上 マイクロ波発生器の電力 同上 マイクロ波の照射時間 同上 延伸機 テンター式延伸機 延伸温度 150℃ 横方向延伸倍率 3.8倍 延伸後の膜厚 18μm 延伸後のフィルム幅 800mm
Example 3 A biaxially stretched laminate was obtained in the same manner as in Example 1 except that the stretching conditions were changed as described below, and the same evaluation was performed. [Primary stretching (longitudinal stretching) conditions] Microwave frequency 2.45 GHz Power of microwave generator 0.2 kW Microwave irradiation time 5 seconds Stretching machine Roll stretching machine Stretching temperature 150 ° C Longitudinal stretching magnification 3. 5 times film thickness after stretching 80 μm [Secondary stretching (transverse stretching) conditions] Microwave frequency Same as above Power of microwave generator Same as above Microwave irradiation time Same as above Stretching machine Tenter type stretching machine Stretching temperature 150 ° C. Lateral stretching Magnification 3.8 times Film thickness after stretching 18 μm Film width after stretching 800 mm

【0019】実施例4 実施例1において、EVOHとして、エチレン含有量4
4モル%、ケン化度99.8モル%のEVOHを用いた
以外は同様に行って、2軸延伸積層体得て、同様に評価
を行った。
Example 4 In Example 1, an ethylene content of 4 was used as EVOH.
A biaxially stretched laminate was obtained in the same manner except that EVOH having 4 mol% and a saponification degree of 99.8 mol% was used, and was similarly evaluated.

【0020】実施例5 実施例1において、ポリプロピレン[日本ポリケム社
製、『ノバテックPPEG8』]層(100μm厚)/
接着樹脂[三井石油化学社製、『アドマー QF50
0』]層(30μm)/EVOH[エチレン含有量32
モル%、ケン化度99.8モル%]層(30μm厚)/
接着樹脂[同上]層(30μm)/低密度ポリエチレン
層(100μm厚)の積層体を用いた以外は同様に行っ
て、2軸延伸積層体得て、同様に評価を行った。
Example 5 In Example 1, a layer of polypropylene [Novatech PPEG8, manufactured by Nippon Polychem Co., Ltd.] (100 μm thick)
Adhesive resin [Mitsui Petrochemical Co., Ltd., "Admer QF50
0 "] layer (30 μm) / EVOH [ethylene content 32
Mol%, saponification degree 99.8 mol%] layer (30 μm thickness) /
A biaxially stretched laminate was obtained in the same manner as above except that a laminate of the adhesive resin [same as above] layer (30 μm) / low-density polyethylene layer (100 μm thickness) was obtained and evaluated in the same manner.

【0021】実施例6 実施例1において、ナイロン[三菱化学社製、『Novami
d 1020』]層(50μm厚)/EVOH[エチレン
含有量32モル%、ケン化度99.8モル%]層(50
μm厚)/ナイロン[三菱化学社製、『Novamid 102
0』]層(50μm厚)の積層体を用いて、第1次延伸
時の延伸温度を130℃、縦延伸倍率を4.5倍、延伸
後の膜厚を45μmとし、第2次延伸時の延伸温度を1
30℃、横延伸倍率を5.2倍、延伸後の膜厚を15μ
mとし、更に熱固定を170℃で7秒とした以外は同様
に行って、2軸延伸積層体得て、同様に評価を行った。
Example 6 In Example 1, nylon [Novami, manufactured by Mitsubishi Chemical Corporation]
d 1020 ″] layer (50 μm thick) / EVOH [ethylene content 32 mol%, saponification degree 99.8 mol%] layer (50
μm thickness) / Nylon [Mitsubishi Chemical's Novamid 102
0 ”] layer (50 μm thick), the stretching temperature in the first stretching is 130 ° C., the longitudinal stretching ratio is 4.5 times, and the film thickness after stretching is 45 μm. Stretching temperature of 1
30 ° C., transverse stretching ratio 5.2 times, film thickness after stretching 15 μm
m, and heat-fixing was performed at 170 ° C. for 7 seconds to obtain a biaxially stretched laminate, which was similarly evaluated.

【0022】実施例7 実施例1と同様の積層体を下記の条件で1軸延伸及び熱
固定を行って、1軸延伸積層体を得て、実施例1と同様
に評価を行った。 [第1次延伸(縦延伸)条件] マイクロ波の周波数 2.45GHz マイクロ波発生器の電力 1.8kw マイクロ波の照射時間 10秒 延伸機 ロール式延伸機 延伸温度 150℃ 縦方向延伸倍率 7.8倍 延伸後の膜厚 35μm 延伸後のフィルム幅 400mm [熱固定条件] 温度 160℃ 時間 5秒
Example 7 The same laminate as in Example 1 was subjected to uniaxial stretching and heat setting under the following conditions to obtain a uniaxially stretched laminate, which was evaluated in the same manner as in Example 1. [Primary stretching (longitudinal stretching) conditions] Microwave frequency 2.45 GHz Power of microwave generator 1.8 kW Microwave irradiation time 10 seconds Stretching machine Roll stretching machine Stretching temperature 150 ° C Longitudinal stretching magnification 7. 8 times Thickness after stretching 35 μm Width of film after stretching 400 mm [Heat setting conditions] Temperature 160 ° C. Time 5 seconds

【0023】比較例1 実施例1において、延伸時にマイクロ波照射を行わずに
延伸を行ったが、高延伸とすることができずに、積層体
に網目状のスジが生じた。実施例の評価結果を表1に示
す。
Comparative Example 1 In Example 1, stretching was performed without performing microwave irradiation at the time of stretching. However, high stretching could not be performed, and network streaks were generated in the laminate. Table 1 shows the evaluation results of the examples.

【0024】[0024]

【表1】 ガスバリヤー性 透明性 引張強度の向上性 (酸素透過度) (ヘイズ値) 実施例1 3.4 1.6 強度向上が認められた 〃 2 4.1 1.4 同 上 〃 3 5.2 1.8 同 上 〃 4 7.4 1.6 同 上 〃 5 4.8 1.5 同 上 〃 6 1.4 1.1 同 上 〃 7 1.7 1.5 同 上 比較例1 >10 35 強度は低下した 註)ガスバリヤー性の単位は、cc/m2・day・atmTable 1 Gas barrier properties Transparency Improvement of tensile strength (oxygen permeability) (Haze value) Example 1 3.4 1.6 Strength improvement was observed {2 4.1 1.4 Same as above} 5.2 1.8 Same as above 4 4 7.4 1.6 Same as above 5 5 4.8 1.5 Same as above 〃 6 1.4 1.1 Same as above 7 7 1.7 1.5 Same as above Comparative example 1> 10 35 Strength decreased Note) The unit of gas barrier property is cc / m 2 · day · atm

【0025】[0025]

【発明の効果】本発明では、EVOHの積層体をマイク
ロ波を照射しながら延伸をしているため、ガスバリヤー
性、透明性、引張強度等に優れた高延伸倍率の延伸積層
体を得ることができ、食品や医薬品、農薬品、工業薬品
等の包装用材料として大変有用である。
According to the present invention, since the EVOH laminate is stretched while being irradiated with microwaves, it is possible to obtain a stretched laminate having a high stretching ratio and excellent gas barrier properties, transparency, tensile strength, and the like. It is very useful as a packaging material for foods, pharmaceuticals, agricultural chemicals, industrial chemicals and the like.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI B29L 9:00 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification code FI B29L 9:00

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 エチレン−酢酸ビニル共重合体ケン化物
層と熱可塑性樹脂層からなる積層体にマイクロ波を照射
しながら延伸することを特徴とする積層体の延伸方法。
1. A method for stretching a laminate, comprising stretching a laminate comprising a saponified ethylene-vinyl acetate copolymer layer and a thermoplastic resin layer while irradiating microwaves.
【請求項2】 エチレン−酢酸ビニル共重合体ケン化物
が、エチレン含量10〜60モル%で、酢酸ビニル成分
のケン化度が90モル%以上であることを特徴とする請
求項1記載の積層体の延伸方法。
2. The laminate according to claim 1, wherein the saponified ethylene-vinyl acetate copolymer has an ethylene content of 10 to 60 mol% and a saponification degree of the vinyl acetate component of 90 mol% or more. Body stretching method.
【請求項3】 熱可塑性樹脂が、ポリオレフィン系樹
脂、ポリアミド系樹脂、ポリエステル系樹脂、ポリスチ
レン系樹脂のいずれかであることを特徴とする請求項1
または2記載の積層体の延伸方法。
3. The resin according to claim 1, wherein the thermoplastic resin is any one of a polyolefin resin, a polyamide resin, a polyester resin, and a polystyrene resin.
Or the stretching method of the laminate according to 2.
【請求項4】 延伸倍率が縦(MD)方向に1.5〜8
倍、横(TD)方向に1.5〜8倍であることを特徴と
する請求項1〜3いずれか記載の積層体の延伸方法。
4. The stretching ratio is 1.5 to 8 in the machine direction (MD).
The stretching method according to any one of claims 1 to 3, wherein the stretching ratio is 1.5 to 8 times in the transverse (TD) direction.
JP1330498A 1998-01-07 1998-01-07 Laminate stretching method Pending JPH11198225A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1330498A JPH11198225A (en) 1998-01-07 1998-01-07 Laminate stretching method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1330498A JPH11198225A (en) 1998-01-07 1998-01-07 Laminate stretching method

Publications (1)

Publication Number Publication Date
JPH11198225A true JPH11198225A (en) 1999-07-27

Family

ID=11829453

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1330498A Pending JPH11198225A (en) 1998-01-07 1998-01-07 Laminate stretching method

Country Status (1)

Country Link
JP (1) JPH11198225A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100584978B1 (en) 2004-12-03 2006-05-29 삼성전기주식회사 Method of manufacturing film type insulating material using high frequency heating
US7581942B2 (en) 2001-10-24 2009-09-01 Ball Corporation Stretch rod for a stretch blow molding machine
RU2483929C2 (en) * 2008-05-21 2013-06-10 Амкор Флексиблз Кройцлинген Лтд. Method of fabricating resilient packing laminate

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7581942B2 (en) 2001-10-24 2009-09-01 Ball Corporation Stretch rod for a stretch blow molding machine
KR100584978B1 (en) 2004-12-03 2006-05-29 삼성전기주식회사 Method of manufacturing film type insulating material using high frequency heating
RU2483929C2 (en) * 2008-05-21 2013-06-10 Амкор Флексиблз Кройцлинген Лтд. Method of fabricating resilient packing laminate

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