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JPH0356168B2 - - Google Patents
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JPH0356168B2 - - Google Patents

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Publication number
JPH0356168B2
JPH0356168B2 JP11253283A JP11253283A JPH0356168B2 JP H0356168 B2 JPH0356168 B2 JP H0356168B2 JP 11253283 A JP11253283 A JP 11253283A JP 11253283 A JP11253283 A JP 11253283A JP H0356168 B2 JPH0356168 B2 JP H0356168B2
Authority
JP
Japan
Prior art keywords
mol
coating
ethylene
vinyl acetate
acetate copolymer
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.)
Expired
Application number
JP11253283A
Other languages
Japanese (ja)
Other versions
JPS602361A (en
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 filed Critical
Priority to JP11253283A priority Critical patent/JPS602361A/en
Publication of JPS602361A publication Critical patent/JPS602361A/en
Publication of JPH0356168B2 publication Critical patent/JPH0356168B2/ja
Granted legal-status Critical Current

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  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
  • Laminated Bodies (AREA)

Description

【発明の詳細な説明】 本発明は酸素等のガスおよび調味料、香料等の
香気成分に対し不透過性の複覆をもつ予備成形物
および該予備成形物を二軸延伸−吹込法により二
軸延伸して得たガス不透過性の二軸延伸中空体に
関する。さらに詳しくいえば予備成形物の少くと
も一つの壁面にエチレン−酢酸ビニル共重合体ケ
ン化物の溶剤溶液の被覆を形成し、次いで該被覆
中の揮発分が0.05〜5重量%となるように乾燥し
たガス不透過性被覆をもつガス不透過性の複合予
備成形物および該複合予備成形物を二軸延伸条件
下で二軸延伸−吹込成形したガス不透過性の二軸
延伸複合中空体に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a preform having a double coating that is impermeable to gases such as oxygen and aromatic components such as seasonings and fragrances, and a biaxially stretching and blowing method for biaxially stretching and blowing the preform. This invention relates to a gas-impermeable biaxially stretched hollow body obtained by axial stretching. More specifically, a coating of a solvent solution of saponified ethylene-vinyl acetate copolymer is formed on at least one wall of the preform, and then dried so that the volatile content in the coating is 0.05 to 5% by weight. The present invention relates to a gas-impermeable composite preform having a gas-impermeable coating and a gas-impermeable biaxially stretched composite hollow body obtained by biaxially stretching and blow molding the composite preform under biaxially stretching conditions.

中空体の分野では近年熱可塑性樹脂が急速な発
展を遂げている。特にポリエチレンテレフタレー
ト系樹脂は予備成形物の二軸延伸吹込成形によつ
て機械的性質(特に耐衝撃性および内圧抵抗性)
に優れたピンを成形する注目すべき特性を持つて
いるので、加圧液体及び発泡飲料の充填に有利に
使用出来ることは周知である。しかしたとえば調
味料、香料が入つていたり、酸素に対する感受性
が高かつたり、炭酸ガスが入つていたり、あるい
はこれらが組合わされているような液体の場合に
は多くの熱可塑性樹脂製中空体のガス及び調味
料、香料に対する不透過性は、不十分である結果
充填された製品は、しばしば限られた期間しか良
好な状態を保ち得ない。ポリエチレンテレフタレ
ート系樹脂、ポリプロピレン系樹脂、ポリスチレ
ン系樹脂等においても例外でない。この現象は中
空体の壁厚が薄いほど、また内容物の体積に対す
る容器の表面積比が高いほど、顕著になる。中空
体の透過率を低下させるために基材よりもガス透
過率の低いバリヤー材を中空体表面に塗布するこ
とが提案されている。さらにポリビニルアルコー
ルがポリエチレン製二軸延伸ピン用表面塗布用バ
リヤー材として使用し、その際、高温度雰囲気下
における欠点を補うために、ポリビニルアルコー
ル被覆に水に不感性で不透過性のポリマーの第2
被覆をほどこす方策なども既に知られている。ま
た有底または無底のパリソン等の予備成形物にポ
リビニルアルコールの被覆をほどこし、これを二
軸延伸吹込法でガス不透過性の二軸延伸複合中空
体とする方法も提案されている。また公知の方法
では被覆は仕上げ容器壁面上に浸漬、噴霧等の塗
布方法を含む各種技術で塗布されるが、塗布層厚
は容器の形が時として複雑となるため、制御する
ことがむづかしいという欠点がある。さらにバリ
ヤー性素材としてポリビニルアルコールが選ばれ
る場合には、製品中空体の表面に塗布する場合、
予備成形物に塗布し、バリヤー材被覆を設け、二
軸延伸吹込法で二軸延伸中空体を得る場合の如何
を問わず、該被覆の耐水性が不十分である点で該
素材の特性に由来する不可避的な欠点がある。該
致命的な欠点を排除するため、ポリビニルアルコ
ールからなる第1被覆層の上に水に不感性で水分
不透過性のポリマーの第2被覆層を設け、第1被
覆層を保護する公知の方法により、湿り雰囲気で
もガス等の透過性を大きく低下させるという方策
がとられてはいるが、実際には乾燥の制御を極め
てむづかしくするという欠点をもつている。すな
わち乾燥が長びくと、たとえば表層の疎水性ポリ
マーのラテツクス中の水分が下層のポリビニルア
ルコール層を再湿潤し、水分不透過性の表層であ
る第2被覆の乾燥が進むことと相俟つて水分不透
過性の被膜が生成し、下層のポリビニルアルコー
ルの乾燥を不完全にとどめてしまう。該現象は下
層のポリビニルアルコールと水との極めて大きい
親和性と表層に使用するポリマーの疎水性により
惹起されるもので不可避的である。
In recent years, thermoplastic resins have made rapid progress in the field of hollow bodies. In particular, polyethylene terephthalate resin has mechanical properties (especially impact resistance and internal pressure resistance) that are improved by biaxial stretch blow molding of preforms.
It is well known that it has the remarkable properties of forming pins with excellent properties and can therefore be used advantageously for the filling of pressurized liquids and sparkling beverages. However, in the case of liquids that contain seasonings, fragrances, are sensitive to oxygen, contain carbon dioxide gas, or a combination of these, many thermoplastic resin hollow bodies are used. Their impermeability to gases and flavorings is inadequate, so that the filled products often remain in good condition for only a limited period of time. Polyethylene terephthalate resins, polypropylene resins, polystyrene resins, etc. are no exception. This phenomenon becomes more pronounced as the wall thickness of the hollow body becomes thinner and as the surface area ratio of the container to the volume of the contents increases. In order to reduce the permeability of the hollow body, it has been proposed to coat the surface of the hollow body with a barrier material having a lower gas permeability than the base material. In addition, polyvinyl alcohol is used as a surface coating barrier material for polyethylene biaxially oriented pins, and in this case, a water-insensitive and impermeable polymer is added to the polyvinyl alcohol coating to compensate for the shortcomings in high temperature atmospheres. 2
Measures such as applying a coating are already known. A method has also been proposed in which a preform, such as a parison with or without a bottom, is coated with polyvinyl alcohol and then made into a gas-impermeable biaxially stretched composite hollow body using a biaxially stretched blowing method. Additionally, in known methods, the coating is applied onto the finished container wall using a variety of techniques including dipping, spraying and other application methods, but the coating layer thickness is difficult to control due to the sometimes complex shape of the container. There are drawbacks. Furthermore, when polyvinyl alcohol is selected as the barrier material, when applied to the surface of the hollow product,
Regardless of whether the preform is coated with a barrier material coating or a biaxially stretched hollow body is obtained by a biaxially stretched blowing method, the water resistance of the coating is insufficient due to the characteristics of the material. There are unavoidable drawbacks that come with it. In order to eliminate this fatal drawback, a known method protects the first coating layer by providing a second coating layer of a water-insensitive and water-impermeable polymer on top of the first coating layer made of polyvinyl alcohol. Although measures have been taken to greatly reduce the permeability of gases etc. even in a humid atmosphere, this actually has the drawback of making drying control extremely difficult. In other words, if drying is prolonged, for example, moisture in the latex of the hydrophobic polymer on the surface layer rewets the polyvinyl alcohol layer below, which in combination with the drying of the second coating, which is the moisture-impermeable surface layer, results in moisture loss. A permeable film is formed and the underlying polyvinyl alcohol is incompletely dried. This phenomenon is inevitable because it is caused by the extremely high affinity between polyvinyl alcohol in the lower layer and water and the hydrophobicity of the polymer used in the surface layer.

エチレン−酢酸ビニル共重合体ケン化物
(EVOHと略記する)系樹脂も酸素、炭酸ガス等
のガスおよび香気成分に対し高いバリヤー性を有
していることも周知の事実であり、前記のポリビ
ニルアルコール系樹脂に比し耐湿性も良好で好適
なバリヤー材としてフイルム等の成形品として他
の熱可塑性樹脂を組合せて用いられている。しか
しこれらの成形品は他の熱可塑性樹脂と、たとえ
ば共押出技術、ドライラミネーシヨン等で積層さ
れてそのまま共延伸されることなく用いられ、あ
るいは他の樹脂製フイルムまたは容器に塗布し、
乾燥し、該容器等の表面にEVOH系樹脂被覆を
設けて各種用途に供せられるものである。また
EVOH系樹脂を積層した予備成形物を得てこれ
を共延伸し、積層物の特性を向上させることおよ
び共押出技術によつて得られるパリソンを二軸延
伸吹込法によつて中空体を得ることは特開昭53−
108162号公報などに僅かに開示されているのみ
で、殆んど見当らない。特に前述の如く、たとえ
ばポリエチレンテレフタレート系樹脂は予備成形
物の二軸延伸吹込成形によつて機械的性質を高め
て加圧液体及び発泡飲料の中空容器として好適に
使用され始めたが、未だ該中空体の湿り雰囲気下
でガス等の不透過性の向上を目的としたEVOH
系樹脂を積層させた二軸延伸吹込成形に際し、好
適に共延伸することが出来る予備成形物は見出さ
れていない。この理由については種々考えられる
が、一つにはEVOH系樹脂の結晶化速度が極め
て大きいこと、予備成形物であるため、延伸後に
目的とする被覆厚みとなる如く、EVOH系被覆
層を厚くせざるを得ず、その結果該被覆をもつ予
備成形物を共押出技術等により積層させて得る場
合、急冷等によりEVOH系樹脂の結晶化を防止
または十分に遅延させることが極めてむづかし
く、ポリエチレン・テレフタレート等の他の熱可
塑性樹脂と共延伸可能な程度に結晶化度をとどめ
ることが極めて困難であることにある。前記特開
昭53−108162号公報等に開示の方法もこの域を出
ない。
It is also a well-known fact that saponified ethylene-vinyl acetate copolymer (abbreviated as EVOH) resins also have high barrier properties against gases such as oxygen and carbon dioxide, and aromatic components. It also has better moisture resistance than other thermoplastic resins, and is used in combination with other thermoplastic resins as a suitable barrier material for molded products such as films. However, these molded products can be laminated with other thermoplastic resins, for example by coextrusion technology, dry lamination, etc., and used as is without being co-stretched, or they can be applied to other resin films or containers, and
After drying, an EVOH resin coating is provided on the surface of the container, etc., and the container is used for various purposes. Also
To obtain a preformed product laminated with EVOH resin and co-stretch it to improve the properties of the laminate, and to obtain a hollow body by biaxial stretching blowing method from a parison obtained by coextrusion technology. is published in Japanese Patent Application Publication No. 1973-
It is only slightly disclosed in Publication No. 108162, etc., and can hardly be found. In particular, as mentioned above, for example, polyethylene terephthalate resins have been improved in mechanical properties by biaxial stretch blow molding of preforms and have begun to be suitably used as hollow containers for pressurized liquids and foamed beverages. EVOH for the purpose of improving the impermeability of gases etc. in the humid atmosphere of the body
No preform has been found that can be suitably co-stretched during biaxial stretch blow molding in which resins are laminated. There are various possible reasons for this, but one is that the crystallization rate of the EVOH resin is extremely high, and because it is a preformed product, the EVOH coating layer must be thick enough to achieve the desired coating thickness after stretching. As a result, when preforms with such a coating are obtained by laminating them by coextrusion technology, it is extremely difficult to prevent or sufficiently delay the crystallization of the EVOH resin by quenching, etc. - It is extremely difficult to maintain the crystallinity to a level that allows co-stretching with other thermoplastic resins such as terephthalate. The method disclosed in the above-mentioned Japanese Patent Application Laid-Open No. 53-108162 and the like does not go beyond this range.

耐水性を有し湿り雰囲気下で好適なガス不透過
性をもつバリヤー材としてEVOH系樹脂を採用
し、かつ熱可塑性樹脂、特にポリエチレンテレフ
タレート系樹脂と複合化し、好適に共延伸するこ
とができる予備成形物が強く望まれている。
EVOH resin is used as a barrier material that is water resistant and has suitable gas impermeability in a humid atmosphere, and is composited with thermoplastic resin, especially polyethylene terephthalate resin, and is a preliminary material that can be suitably co-stretched. Molded products are strongly desired.

本発明者らは該従来技術の欠点を排除し、耐水
性を有し、湿り雰囲気でも酸素・炭素ガス等のガ
スおよび香気成分に対して充分な不透過性を示す
二軸延伸中空体を得ることを目的として、バリヤ
ー材であるEVOH系樹脂とポリエチレンテレフ
タレート系樹脂、ポリプロピレン系樹脂、ポリス
チレン系の樹脂、ポリ塩化ビニル系樹脂等の熱可
塑性樹脂との積層物についてその共延伸性に重点
をおき、鋭意検討を行なつた結果、好適に共延伸
可能なEVOH系樹脂と他の熱可塑性樹脂との複
合構成をもつ二軸延伸中空体製造用予備成形物を
完成し、耐水性を有し、湿り雰囲気でも好適な酸
素等に対する不透過性をもつ二軸延伸中空体を提
供することを可能とした。すなわち本発明の複合
予備成形物および二軸延伸複合中空体は少くとも
一つの壁面がEVOH系樹脂の溶剤溶液の被覆を
形成し、次いで該被覆中の揮発分が0.05〜5重量
%となるように乾燥したガス不透過性被覆をもつ
予備成形物であり、さらに該予備成形物を二軸延
伸条件下に共延伸して得られる複合中空体であ
る。
The present inventors eliminate the drawbacks of the prior art and obtain a biaxially stretched hollow body that is water resistant and exhibits sufficient impermeability to gases such as oxygen and carbon gases and aroma components even in a humid atmosphere. For this purpose, we focused on the co-stretchability of laminates of EVOH resin, which is a barrier material, and thermoplastic resins such as polyethylene terephthalate resin, polypropylene resin, polystyrene resin, and polyvinyl chloride resin. As a result of extensive research, we have completed a preform for manufacturing biaxially stretched hollow bodies that has a composite structure of EVOH resin and other thermoplastic resin that can be co-stretched, and has water resistance. This makes it possible to provide a biaxially stretched hollow body that has suitable impermeability to oxygen and the like even in a humid atmosphere. That is, in the composite preform and biaxially stretched composite hollow body of the present invention, at least one wall surface is coated with a solvent solution of EVOH resin, and then the volatile content in the coating is 0.05 to 5% by weight. The composite hollow body is obtained by co-stretching the preform under biaxial stretching conditions.

ここで本発明における揮発分は乾量基準の値で
ある。該溶剤としては100℃以下の比較的低温で
EVOH系樹脂を溶解し得る溶剤が該樹脂溶液を
塗布する作業性等から好適に用いられる。たとえ
ばアルコール系溶剤としてはメタノール/水系、
エタノール/水系、n−プロピルアルコール/水
系、i−プロピルアルコール/水系、t−ブチル
アルコール/水系などがあり、またこれらのアル
コールの2種以上と水の混合物も好適に用いるこ
とができる。また、これらのアルコール水溶液は
均一に混り合う組成領域内で水を部分溶解する脂
肪族アルコール、たとえばn−ブチルアルコー
ル、i−ブチルアルコール、sec−ブチルアルコ
ールなどを、更に難溶性の該アルコール類、たと
えばn−、i−、t−の各アミルアルコール等を
含んでいてもよい。しかし、水と部分溶解性また
は難溶性を示すアルコールが混在する場合には複
合予備成形物の部分乾燥上水と均一に溶け合わな
い組成領域に至る場合が生じて得られる被覆の透
明性が低下する場合があり、好適に用いることの
できる範囲はかなり狭いものとなる。
Here, the volatile content in the present invention is a value on a dry basis. The solvent is relatively low temperature below 100℃.
A solvent that can dissolve the EVOH resin is preferably used from the viewpoint of workability in applying the resin solution. For example, alcohol solvents include methanol/water,
Examples include ethanol/water system, n-propyl alcohol/water system, i-propyl alcohol/water system, t-butyl alcohol/water system, and mixtures of two or more of these alcohols and water can also be suitably used. In addition, these alcohol aqueous solutions contain aliphatic alcohols that partially dissolve water, such as n-butyl alcohol, i-butyl alcohol, sec-butyl alcohol, etc., in a uniformly mixed composition region, and the alcohols that are less soluble. , for example, n-, i-, and t-amyl alcohols. However, when water and alcohol that is partially soluble or poorly soluble coexist, a composition region may be reached that does not uniformly dissolve in the partially dried water of the composite preform, resulting in a decrease in the transparency of the resulting coating. In some cases, the range of suitable use is quite narrow.

なお上記n−はノルマルを、i−はイソを、
sec−はセカンダリーを、t−はタ−シヤリーを
意味する。
In addition, the above n- stands for normal, i- stands for iso,
sec- means secondary and t- means tertiary.

透明な被覆を得るためのEVOH系樹脂のアル
コール/水系組成物は、該樹脂をn−プロピルア
ルコール/水系、i−プロピルアルコール/水
系、t−ブチルアルコール/水系に溶解して得る
ことができる。しかしこれらのアルコール/水系
溶媒においてもEVOH系樹脂のエチレン含量に
応じて、その組成を選択しなければ、透明な塗膜
を形成させ得ない。n−プロピルアルコール、i
−プロピルアルコールおよびt−ブチルアルコー
ルの場合、該樹脂のエチレン含量との関連におい
て好適なアルコール/水系溶媒の組成範囲が特公
昭47−48489号公報に開示されている。EVOH系
樹脂をフイルム、ビン系の成形物に塗布し、乾燥
して、酸素等のバリヤー性を高めた成形品とする
ことは該公報にも開示され公知である。この場合
における乾燥後の揮発分はEVOH系樹脂が水分
を含むと、そのガス不透過性が低下するために通
常0.3%以下、好ましくは0.1%以下の極めて低領
域になる如く配慮が行われかつ、さらに熱処理が
なされるのを通常としている。このために本発明
の目的とする複合化された予備成形物に単純に
EVOH系樹脂のアルコール/水系組成物を塗布
して該樹脂の被覆を他の熱可塑性樹脂に形成させ
て得た後、これを二軸延伸吹込法で共延伸して特
性を向上させた中空体を得ることは前述の如く
EVOH系樹脂の結晶化速度が大きく極めて困難
であり、なお解決を要する重大な課題であつた。
すなわち、たとえば該複合化されたシートは乾燥
後のEVOH系樹脂の結晶化度が高いため、共延
伸を好適に行うことができない。また本発明者ら
はEVOH系樹脂の層で被覆された熱可塑性樹脂
製二軸延伸中空体製造用予備成形物を得る目的で
該組成領域のアルコールの樹脂溶液を、たとえば
ポリエチレンテレフタレート樹脂に塗布し乾燥し
て行つたところ、得られた該複合された有底また
は無底のバリソン等の予備成形物は二軸延伸条件
下で二軸延伸吹込操作において該ポリエステル樹
脂部のみ延伸され、EVOH系樹脂の被覆層は、
殆んど延伸されなかつた。さらに驚くべきことに
該操作で塗布した後、該被覆層内の揮発分を0.3
ないし5重量%にとどめるよう乾燥操作を制御し
て行つたところ、二軸延伸吹込操作で完全に満足
しうる共延伸性に示し、透明で、かつ湿り雰囲気
において満足なガス不透過性をもつ、二軸延伸中
空体を得ることができることを見出した。従来
EVOH系樹脂の二軸延伸フイルムを得るに当つ
て原反を再調湿し、水分率を規定して行わねば好
適に延伸できないという事実は広く知られてい
る。しかし該二軸延伸中空体を得るに当つて、予
備成形物にEVOH系樹脂溶液を塗布し、0.1重量
%の揮発分になる如く乾燥した後、再度水分を付
与して揮発分を0.3ないし5重量%になる如く調
整した後、二軸延伸吹込操作に供したところ、本
発明の予備成形物を用いた場合に比し、共延伸性
は極めて不満足なもので殆んど延伸出来ないか不
均一度が極めて大きく、延伸されない部分、中途
半端にしか延伸されない状態を示す部分等が髄所
に見られたり、被覆が破れたりしたものであつ
た。本発明においては、該被覆を形成させるに当
つてとくにアルコール/水系という2成分系溶剤
を用い、かつ乾燥後の揮発分を好適量残存せしめ
ることによつて前述のような欠点を解消すること
ができる。これは詳しくは明らかでないが、該揮
発分中に該アルコール成分を含むことに起因する
ものとみられる。このことは、溶剤がアルコー
ル/水系であると揮発分が0.05重量%以下になる
と、該作用効果が発現され難くなること、またた
とえば前述のアミルアルコール等の比較的高沸点
をもつアルコール、後述の高沸点の非アルコール
系溶剤を少量添加して用いるときには、これらの
成分が残存揮発分中に残り易く、該複合予備成形
物の部分乾燥時の共延伸性付与のための必要残存
揮発分量を減少させ得る事などからも示唆され
る。
An alcohol/water based EVOH resin composition for obtaining a transparent coating can be obtained by dissolving the resin in an n-propyl alcohol/water system, an i-propyl alcohol/water system, or a t-butyl alcohol/water system. However, even in these alcohol/aqueous solvents, a transparent coating film cannot be formed unless the composition is selected depending on the ethylene content of the EVOH resin. n-propyl alcohol, i
- In the case of propyl alcohol and t-butyl alcohol, the suitable composition range of alcohol/aqueous solvent in relation to the ethylene content of the resin is disclosed in Japanese Patent Publication No. 47-48489. This publication also discloses that it is known to apply EVOH resin to a molded product such as a film or a bottle and dry it to obtain a molded product with improved barrier properties against oxygen and the like. In this case, care is taken to keep the volatile content after drying in the extremely low range of usually 0.3% or less, preferably 0.1% or less, because when the EVOH resin contains moisture, its gas impermeability decreases. , it is customary to further perform heat treatment. For this purpose, the composite preform which is the object of the invention is simply
A hollow body obtained by applying an alcohol/water based composition of EVOH resin to form a coating of the resin on another thermoplastic resin, and then co-stretching this using a biaxial stretching blowing method to improve properties. As mentioned above, obtaining
The crystallization rate of EVOH-based resins is high and it is extremely difficult to solve this problem, which remains a serious problem that still needs to be solved.
That is, for example, since the EVOH resin in the composite sheet has a high degree of crystallinity after drying, co-stretching cannot be suitably performed. In addition, the present inventors applied a resin solution of an alcohol in the composition range to, for example, polyethylene terephthalate resin in order to obtain a preform for manufacturing a biaxially stretched hollow body made of thermoplastic resin coated with a layer of EVOH resin. When dried, the resulting composite preform, such as a bottomed or bottomless balisong, was stretched in a biaxial stretching blowing operation under biaxial stretching conditions, and only the polyester resin portion was stretched, resulting in an EVOH resin. The coating layer of
It was hardly stretched. Even more surprisingly, after application in this operation, the volatile content in the coating layer was reduced to 0.3
When the drying operation was controlled to keep the amount from 5 to 5% by weight, it showed completely satisfactory co-stretchability in the biaxial stretching blowing operation, was transparent, and had satisfactory gas impermeability in a humid atmosphere. It has been found that a biaxially stretched hollow body can be obtained. Conventional
It is widely known that in order to obtain a biaxially stretched film of EVOH resin, the film cannot be stretched properly unless the film is re-humidified and the moisture content is regulated. However, in order to obtain the biaxially stretched hollow body, an EVOH resin solution is applied to the preform, dried to a volatile content of 0.1% by weight, and then water is added again to reduce the volatile content to 0.3 to 5% by weight. When the preform was adjusted to the desired weight percentage and then subjected to a biaxial stretching blowing operation, the co-stretchability was extremely unsatisfactory compared to the case of using the preform of the present invention, and the result was that it could hardly be stretched or could not be stretched. The degree of uniformity was extremely high, and there were parts that were not stretched, parts that were only half-stretched, etc. in the medullary region, and the coating was torn. In the present invention, the above-mentioned drawbacks can be overcome by using a two-component alcohol/water solvent in forming the coating, and by allowing a suitable amount of volatile matter to remain after drying. can. Although the details of this are not clear, it is believed that this is due to the inclusion of the alcohol component in the volatile matter. This means that if the solvent is alcohol/water-based and the volatile content is less than 0.05% by weight, it will be difficult to achieve the desired effect. When a small amount of a high boiling point non-alcoholic solvent is added and used, these components tend to remain in the residual volatile matter, reducing the amount of residual volatile matter necessary for imparting co-stretchability during partial drying of the composite preform. This is also suggested by the fact that it can be caused.

本発明にアルコール/水系溶剤を用いる場合に
は、該予備成形物の部分乾燥後の揮発分は、0.05
〜5重量%、好ましくは0.1〜5重量%、さらに
好ましくは0.3〜5重量%、最適には0.5〜5重量
%である場合に、好適に該複合予備成形物を二軸
延伸条件下で二軸延伸−吹込法で共延伸すること
ができる。該揮発分が0.05重量%以下であれば良
好な共延伸性を示さず、また5重量%以上では、
中空体成形時に発泡現象の恐れがあり、さらに二
軸延伸効果による被覆の特性の向上も期待できな
い。
When an alcohol/aqueous solvent is used in the present invention, the volatile content after partial drying of the preform is 0.05
Preferably the composite preform is biaxially stretched under biaxial stretching conditions when the amount is 5% by weight, preferably 0.1-5% by weight, more preferably 0.3-5% by weight, optimally 0.5-5% by weight. Co-stretching can be performed by an axial stretching-blow method. If the volatile content is 0.05% by weight or less, good co-stretchability is not exhibited, and if it is 5% by weight or more,
There is a risk of foaming during molding of the hollow body, and furthermore, improvement in coating properties due to the biaxial stretching effect cannot be expected.

本発明においては溶剤として非アルコール系溶
剤を用いることもできる。好適な非アルコール系
溶剤としては、ジメチルスルホキシド、N−メチ
ルー2−ピロリドン、ジメチルフオルムアミド、
0〜20重量%含水フエノール、メタクレゾール、
エチレンクロルヒドリンなどがある。これらの非
アルコール系溶剤は、EVOH系樹脂の溶剤とし
ては優れたものであり、溶解性の点ではアルコー
ル系溶剤に優り、常に容易に透明な被覆をうるこ
とができる。しかし、沸点が高く、該複合予備成
形物の部分乾燥時および該複合中空体形成後の残
留溶剤成分の除去時には、たとえばポリエチレン
テレフタレート、ポリプロピレン、ポリスチレ
ン、ポリ塩化ビニル等の熱可塑性樹脂の耐熱性等
の制約からまた前者の場合には、その他に該樹脂
の結晶化の観点からの制約からも比較的低温の乾
燥が要求されるために減圧乾燥によらねばならな
い場合が多いという欠点がある。たとえばポリエ
チレンテレフタレート製の複合パリソンなどの予
備成形物の乾燥時には、約130℃以下、該パリソ
ンから得た二軸延伸中空体の被覆中の残留溶剤成
分の除去時には、約70℃以下の該熱可塑性樹脂の
温度で行う必要があり、たとえばジメチルスルホ
キシド(沸点85〜87℃/25mmHg)の場合などか
なりの減圧下での乾燥が要求される。
In the present invention, a non-alcoholic solvent can also be used as the solvent. Suitable non-alcoholic solvents include dimethylsulfoxide, N-methyl-2-pyrrolidone, dimethylformamide,
0 to 20% by weight hydrated phenol, metacresol,
Examples include ethylene chlorohydrin. These non-alcoholic solvents are excellent as solvents for EVOH resins, superior to alcoholic solvents in terms of solubility, and can always easily provide a transparent coating. However, due to its high boiling point, heat resistance of thermoplastic resins such as polyethylene terephthalate, polypropylene, polystyrene, polyvinyl chloride, etc. is In addition, in the former case, there is a drawback that drying at a relatively low temperature is required due to other constraints from the viewpoint of crystallization of the resin, and thus drying under reduced pressure must be used in many cases. For example, when drying a preform such as a composite parison made of polyethylene terephthalate, the temperature is about 130°C or less, and when removing the residual solvent component in the coating of a biaxially stretched hollow body obtained from the parison, the temperature is about 70°C or less. It is necessary to carry out the drying at the temperature of the resin, and, for example, in the case of dimethyl sulfoxide (boiling point 85-87°C/25 mmHg), drying is required under considerable reduced pressure.

非アルコール系溶剤の場合、複合予備成形物の
部分乾燥後の揮発分は0.05〜3重量%、好ましく
は0.1〜3重量%である場合に好適に複合予備成
形物を二軸延伸条件下で二軸延伸吹込法で共延伸
できる。しかしながら該揮発分が0.05重量%以下
では良好な共延伸性を示さず、また3重量%以上
では、二軸延伸効果による該被覆の特性の向上が
期待できない。このように該非アルコール溶剤の
場合にはアルコール/水系溶剤の場合に比し、低
揮発分領域に好適な範囲がある。けだし溶剤性が
アルコール/水系溶剤に優れるからである。また
該非アルコール系溶剤の少量を前記アルコール/
水系溶剤に添加混在せしめて用いることは、良好
な共延伸性を付与させる点で好ましく、この場合
複合予備成形物の部分乾燥後の揮発分が低い領域
においても良好な共延伸性を示す。
In the case of non-alcoholic solvents, the composite preform is preferably biaxially stretched under biaxial stretching conditions when the volatile content of the composite preform after partial drying is 0.05 to 3% by weight, preferably 0.1 to 3% by weight. Co-stretching can be performed using the axial stretching blowing method. However, if the volatile content is less than 0.05% by weight, good co-stretchability is not exhibited, and if it is more than 3% by weight, no improvement in the properties of the coating due to the biaxial stretching effect can be expected. As described above, in the case of the non-alcoholic solvent, there is a suitable range in the low volatile content region compared to the case of alcohol/aqueous solvents. This is because the solvent properties are superior to alcohol/aqueous solvents. In addition, a small amount of the non-alcoholic solvent is added to the alcohol/
It is preferable to use it by adding it to an aqueous solvent in order to impart good co-stretchability, and in this case, good co-stretchability is exhibited even in a region where the volatile content after partial drying of the composite preform is low.

本発明に用いるEVOH系樹脂の該溶剤溶液は
おける該樹脂濃度が5〜30重量%、好ましくは10
〜25重量%の範囲のものが好適に用いることがで
きる。EVOH系樹脂は低エチレン含量の組成領
域にあつては耐水性においてポリビニルアルコー
ルに比し優るものの、湿り雰囲気下でのバリヤー
性は未だ満足するものとはなり得ず、また高エチ
レン含量の組成領域にあつては耐水性に優れるも
のの、バリヤー性が低下するために不満足なもの
となる。本発明には、エチレン含量25ないし60モ
ル%の組成領域のEVOH系樹脂が好適に用いら
れる。単一の被覆層にあつては酸素等に対するバ
リヤー性を重視する用途分野を対象とする場合に
は該組成物領域の中でも低エチレン含量領域たと
えば(B)エチレン含量25ないし35モル%、ケン化度
96モル%以上のEVOH系樹脂を、また耐湿性を
重視する用途分野を対象とする場合には、該組成
領域内の高エチレン含量領域、たとえば(C)エチレ
ン含量40ないし60モル%、ケン化度96モル%以上
のEVOH系樹脂が好適に用いられる。前記の場
合、湿り雰囲気下における酸素等に対するバリヤ
ー性の低下をより一層抑制するためには該
EVOH系樹脂被覆層を2層構造とすること、つ
まり(B)エチレン含量25ないし35モル%、ケン化度
96モル%以上のEVOH系樹脂を被覆し、次いで
(C)エチレン含量40ないし60モル%、ケン化度96モ
ル%以上のEVOH系樹脂を被覆することがより
好適である。いづれの層を内側に設けるかについ
ては該中空体に充填される物の性質、状態、該被
覆をほどこす熱可塑性樹脂の種別、該中空体外面
が接する雰囲気等により決定される。たとえばビ
ール、コーラなどの水性混合物が内容物であると
きには該熱可塑性樹脂部の透湿性が前記EVOH
系樹脂層のいづれよりも小さい場合には、低エチ
レン含量EVOH系樹脂(B)層を内側に、高エチレ
ン含量EVOH系樹脂(C)層を外側に設けることが
好ましく、また該熱可塑性樹脂部の透湿性が低エ
チレン含量EVOH系樹脂層の透湿性よりも小さ
く、高エチレン含量のEVOH系樹脂層のそれよ
り大きい場合には、前記の場合の逆の位置に2種
のEVOH系樹脂層を設けることが好適である。
EVOH系樹脂の2層構造の被覆は、予備成形物
に先づ第1層を塗布し、予備乾燥を行つた後、第
2層を塗布し、乾燥するに当り、両層内の揮発分
が0.05ないし5重量%になる如く行うことにより
2層構造の被覆を得ることができる。
The solvent solution of the EVOH resin used in the present invention has a resin concentration of 5 to 30% by weight, preferably 10% by weight.
25% by weight can be suitably used. Although EVOH resins are superior to polyvinyl alcohol in terms of water resistance in compositions with low ethylene content, their barrier properties in humid atmospheres are still unsatisfactory, and in compositions with high ethylene content. Although it has excellent water resistance, it is unsatisfactory due to a decrease in barrier properties. In the present invention, an EVOH resin having an ethylene content of 25 to 60 mol% is preferably used. In the case of a single coating layer, if the target is a field of application that emphasizes barrier properties against oxygen, etc., a low ethylene content region (B) ethylene content of 25 to 35 mol%, saponification, etc. Every time
When using EVOH resins with an EVOH content of 96 mol% or more, and in applications where moisture resistance is important, high ethylene content areas within the composition range, such as (C) ethylene content of 40 to 60 mol%, saponification An EVOH resin having a concentration of 96 mol% or more is preferably used. In the above case, in order to further suppress the deterioration of barrier properties against oxygen etc. in a humid atmosphere,
The EVOH resin coating layer should have a two-layer structure, that is, (B) ethylene content of 25 to 35 mol%, saponification degree
Covered with EVOH resin of 96 mol% or more, then
(C) It is more preferable to coat with an EVOH resin having an ethylene content of 40 to 60 mol% and a saponification degree of 96 mol% or more. Which layer is provided on the inside is determined by the nature and condition of the material to be filled in the hollow body, the type of thermoplastic resin used to coat the hollow body, the atmosphere with which the outer surface of the hollow body comes into contact, and other factors. For example, when the content is an aqueous mixture such as beer or cola, the moisture permeability of the thermoplastic resin part is
If the thermoplastic resin layer is smaller than either of the thermoplastic resin layers, it is preferable to provide the low ethylene content EVOH resin (B) layer on the inside and the high ethylene content EVOH resin (C) layer on the outside. If the moisture permeability of the EVOH resin layer with a low ethylene content is lower than that of the EVOH resin layer with a high ethylene content, two types of EVOH resin layers may be placed in opposite positions to those in the above case. It is preferable to provide one.
A two-layer coating of EVOH resin involves first applying the first layer to the preform, pre-drying it, then applying the second layer, and drying it. By adjusting the amount to 0.05 to 5% by weight, a two-layer coating can be obtained.

予備成形物への塗布は、たとえば浸漬、ドクタ
ーコーター、スプレー、噴霧等の任意の公知の手
段で実施できる。湿りと接着を容易にするため、
例えばコロナ放電処理、火災処理の予備表面処理
を行うことができる。また予備成形物の壁面上に
接着剤層を前以つて設けておくなどの方法を採る
ことは、より好適に行うことができる。接着剤と
しては、エチレン−酢酸ビニル共重合体、または
その不飽和カルボン酸若しくは該酸の無水物のグ
ラフト物などの該共重合体の変性物、ポリウレタ
ン系樹脂などが好適に用いることが出来る。
Coating to the preform can be carried out by any known means such as dipping, doctor coater, spraying, atomizing, etc. To facilitate wetting and adhesion,
For example, corona discharge treatment and preliminary surface treatment for fire treatment can be performed. Further, it is more suitable to adopt a method such as providing an adhesive layer on the wall surface of the preform in advance. As the adhesive, ethylene-vinyl acetate copolymers, modified products of the copolymers such as graft products of unsaturated carboxylic acids or anhydrides thereof, polyurethane resins, and the like can be suitably used.

前記EVOH系樹脂層の内層として、さらに(A)
エチレン含量25ないし60モル%、ケン化度85ない
し95モル%のEVOH系樹脂層を設けることは他
の接着剤層を前以つて設けない場合などに、他の
熱可塑性樹脂との接着性を一層向上させ得るの
で、より好適である。
As an inner layer of the EVOH resin layer, (A)
Providing an EVOH resin layer with an ethylene content of 25 to 60 mol% and a saponification degree of 85 to 95 mol% improves adhesion with other thermoplastic resins when no other adhesive layer is previously provided. This is more preferable because it can further improve the performance.

本発明に用いるEVOH系樹脂は公知の如くエ
チレン−酢酸ビニル系共重合体をたとえばアルカ
リ等の存在下にケン化して得られるが該ケン化度
は、前記接着性向上剤として用いる場合を除き、
96モル%以上好ましくは98モル%以上が好適であ
る。ケン化度が96モル%以下になると、酸素等に
対するバリヤー性および耐水性が低下し不満足な
ものとなる。
The EVOH resin used in the present invention is obtained by saponifying an ethylene-vinyl acetate copolymer in the presence of an alkali, etc., as is known in the art.
It is preferably 96 mol% or more, preferably 98 mol% or more. When the degree of saponification is less than 96 mol%, the barrier properties against oxygen and the like and water resistance decrease, resulting in unsatisfactory results.

塗布する被覆組成物の量は該複合予備成形物の
二軸延伸−吹込み操作中に生ずる厚さの減少を考
慮して選択する必要がある。予備成形物上の被覆
重量は一般に乾燥材料基準で、たとえば10ないし
200g/m2である。乾燥手段としては高温の空気
若しくは窒素などの不活性ガスまたは、所要の波
長の赤外線幅射(たとえば平均波長2μ)を用い
る装置を用いることができる。二軸延伸EVOH
系樹脂薄膜の形成は、揮発分含量が0.05ないし5
重量%、好ましくは該アルコール/水系溶剤の場
合には、0.3〜5重量%、最適には0.5〜5重量
%、該非アルコール溶剤の場合には、好ましくは
0.05ないし3重量%、最適には0.1〜3重量%に
制御された乾燥を行うことによつて容易に行うこ
とができ、該部分乾燥後の該予備成形物の被覆は
良好な共延伸性をもつ。乾燥条件は該要件を満
し、発泡等の現象を生じず連続な相である被覆を
得られるよう任意に選定し行うことができる。該
アルコール/水系溶剤を用いる場合には、50℃以
上、該溶剤系の沸点以下の被覆層の温度に保持し
て行うことが好ましい。また熱可塑性樹脂の結晶
化温度以下の温度領域で行うことが両樹脂の結晶
化を抑制するために必要である。
The amount of coating composition applied should be selected to take into account the thickness reduction that occurs during the biaxial stretch-blow operation of the composite preform. The coating weight on the preform is generally on a dry material basis, e.g.
It is 200g/ m2 . As the drying means, it is possible to use high temperature air, an inert gas such as nitrogen, or a device using infrared radiation of a desired wavelength (for example, an average wavelength of 2 μm). Biaxially stretched EVOH
The formation of a thin film of the resin based on the volatile content is 0.05 to 5.
% by weight, preferably from 0.3 to 5% by weight in the case of the alcohol/aqueous solvent, optimally from 0.5 to 5% by weight in the case of the non-alcoholic solvent.
This can be easily done by controlling drying to 0.05 to 3% by weight, optimally 0.1 to 3% by weight, and the coating of the preform after partial drying has good co-stretchability. Motsu. The drying conditions can be arbitrarily selected so as to satisfy the requirements and to obtain a continuous phase coating without causing phenomena such as foaming. When using the alcohol/aqueous solvent, it is preferable to maintain the temperature of the coating layer at 50° C. or higher and below the boiling point of the solvent. Further, it is necessary to perform the treatment in a temperature range below the crystallization temperature of the thermoplastic resin in order to suppress crystallization of both resins.

このようにして得られた該複合予備成形物は次
いで通常の方法、たとえば有底パリソンをブロー
成形機の金型内に設置し、加熱して所定の倍率ま
で二軸延伸する方法などで通常の圧力温度条件下
たとえばポリエチレンテレフタレート樹脂の場合
ガラス転移温度と結晶化温度の範囲内で、すなわ
ち80〜130℃の間で二軸延伸中空体に転換する。
中空体の形成後、該被覆の乾燥を行い、残留揮発
分を除去し、要すれば該被覆の熱処理を行う。該
乾燥および熱処理は該中空体を形成する二軸延伸
された熱可塑性樹脂部の耐熱温度以下で、たとえ
ばポリエチレンテレフタレートの場合、該樹脂部
の温度が約70℃以上の温度にならないよう行わね
ばならない。
The composite preform thus obtained is then processed in a conventional manner, such as by placing a bottomed parison in the mold of a blow molding machine, heating it, and biaxially stretching it to a predetermined magnification. Under pressure and temperature conditions, for example in the case of polyethylene terephthalate resins, within the range of the glass transition temperature and the crystallization temperature, ie between 80 DEG and 130 DEG C., the conversion into biaxially oriented hollow bodies occurs.
After the formation of the hollow body, the coating is dried to remove residual volatiles and, if necessary, heat-treated. The drying and heat treatment must be carried out at a temperature below the heat resistance temperature of the biaxially stretched thermoplastic resin part forming the hollow body, and in the case of polyethylene terephthalate, for example, the temperature of the resin part must be carried out so that the temperature does not exceed about 70°C. .

得られる該中空体は、極めて良好な酸素等に対
するバリヤー性を有しかつ湿度依存性も小さい。
The resulting hollow body has extremely good barrier properties against oxygen and the like, and has low humidity dependence.

下記に実施例にもとづき本発明の詳細を説明す
るがその範囲を限定するものではない。なお実施
例中の部は重量部を意味する。
The details of the present invention will be explained below based on Examples, but the scope thereof is not limited. Note that parts in the examples mean parts by weight.

実施例 1 n−プロピルアルコール60部と水40部とからな
る溶媒85部にエチレン含量32モル%、ケン化度
99.8モル%のEVOH樹脂15部を加え80〜85℃の温
度下に撹拌しながら溶解し、透明な溶布液を調整
した。長さ160mm、外径25mm肉厚25mmの射出成形
で得られた固有粘度(25℃、1%クロロホルム溶
液で測定)が0.81dl/gのポリエチレンテレフタ
レートの有底パリソンの外表面をコロナ処理した
後、前記調整した60℃に保持した塗布液に浸漬し
て浸漬法で該パリソンの外表面に該EVOH樹脂
を塗布した。塗布後該被覆層の温度が55℃以上で
塗布液が発泡しない状態を保持していることを確
認しつつ、赤外線幅射(平均波長:2μ)による
予備乾燥を行い、次いで105℃の熱風により乾燥
した。該複合化された有底パリソンの被覆内の揮
発分は2.6重量%であり、該樹脂の純量基準塗布
量は46g/m2であつた。得られた該被覆層をもつ
複合予備成形物を108℃の温度に加熱し、二軸延
伸吹込法により約1.5の内容積をもつ二軸延伸
された複合中空体を得た。該中空体のポリエチレ
ンテレフタレート樹脂部の温度が70℃以上になら
ないように注意しつつ80℃の温風で乾燥した後、
該被覆を190℃で数秒間熱処理した。該被覆層の
厚みは4.6μであつた。該中空体の酸素透過係数は
40℃、相対湿度45%の条件下で2.1×10-13cm3
cm/cm2・seccmHgであつた。共延伸性は良好であ
つた。
Example 1 85 parts of a solvent consisting of 60 parts of n-propyl alcohol and 40 parts of water, with an ethylene content of 32 mol% and a degree of saponification.
15 parts of 99.8 mol % EVOH resin was added and dissolved under stirring at a temperature of 80 to 85°C to prepare a transparent solution. After corona treatment of the outer surface of a bottomed polyethylene terephthalate parison with an intrinsic viscosity (measured in 1% chloroform solution at 25°C) of 0.81 dl/g obtained by injection molding with a length of 160 mm, an outer diameter of 25 mm, and a wall thickness of 25 mm. The EVOH resin was applied to the outer surface of the parison by a dipping method by immersing it in the coating solution prepared above and maintained at 60°C. After coating, while making sure that the temperature of the coating layer is 55℃ or higher and that the coating solution does not foam, preliminary drying is performed using infrared radiation (average wavelength: 2μ), and then drying is carried out using hot air at 105℃. Dry. The volatile content in the coating of the composite bottomed parison was 2.6% by weight, and the pure coating amount of the resin was 46 g/m 2 . The obtained composite preform having the coating layer was heated to a temperature of 108° C., and a biaxially stretched composite hollow body having an internal volume of about 1.5 was obtained by a biaxially stretched blowing method. After drying with hot air at 80°C while being careful not to let the temperature of the polyethylene terephthalate resin part of the hollow body rise above 70°C,
The coating was heat treated at 190°C for a few seconds. The thickness of the coating layer was 4.6μ. The oxygen permeability coefficient of the hollow body is
2.1×10 -13 cm 3 at 40℃ and 45% relative humidity.
cm/ cm2・seccmHg. Co-stretchability was good.

実施例 2 実施例1において酢酸ビニル含量26重量%、無
水マレイン酸含量1.5重量%の無水マレイン酸変
性エチレン酢酸ビニル共重合体からなる接着剤の
10g/m2の量で外表面が被覆されたポリエチレン
テレフタレート製有底パリソンを用い、また
EVOH樹脂溶液の調整に当り、n−アミルアル
コールをn−プロピルアルコール/水混合溶媒
100部に対し3部添加して行い、該樹脂の純量基
準で塗布量を85g/m2とした以外は実施例1と同
様に操作した。塗布操作は予備乾燥をはさんで2
回実施した。該被覆の乾燥後の揮発分は、4.2重
量%であり、該複合パリソンを二軸延伸−吹込に
供した。共延伸性は良好であり、得られた複合中
空体の該被覆層の厚みは8.6μであり、該中空体の
酸素透過係数は35℃、相対湿度45%の条件下で
1.1×10-13cm3・cm/cm2・sec.cmHgであつた。
Example 2 In Example 1, an adhesive consisting of a maleic anhydride-modified ethylene vinyl acetate copolymer with a vinyl acetate content of 26% by weight and a maleic anhydride content of 1.5% by weight was prepared.
Using a bottomed parison made of polyethylene terephthalate coated on the outer surface with an amount of 10 g/m2,
When preparing the EVOH resin solution, use n-amyl alcohol as an n-propyl alcohol/water mixed solvent.
The same procedure as in Example 1 was carried out except that 3 parts per 100 parts of the resin was added and the coating amount was 85 g/m 2 based on the pure amount of the resin. The coating operation is done in 2 steps with preliminary drying in between.
Conducted twice. The volatile content of the coating after drying was 4.2% by weight, and the composite parison was subjected to biaxial stretching-blowing. The co-stretchability was good, the thickness of the coating layer of the obtained composite hollow body was 8.6μ, and the oxygen permeability coefficient of the hollow body was 35°C and 45% relative humidity.
It was 1.1×10 -13 cm 3・cm/cm 2・sec.cmHg.

実施例 3 実施例1においてEVOH樹脂を塗布した後、
乾燥した予備成形物の被覆中の水分率を、0.8重
量%、3.2重量%、および4.7重量%のそれぞれに
部分乾燥して行つた以外は、実施例1と同様に行
つた。該被覆の厚さはそれぞれ4.5μ、4.7μ、およ
び4.6μであり共延伸性は良好であつた。該中空体
の酸素透過係数は実施例1における値とほぼ同じ
値であつた。
Example 3 After applying EVOH resin in Example 1,
The procedure of Example 1 was repeated, except that the moisture content in the coating of the dried preform was partially dried to 0.8% by weight, 3.2% by weight, and 4.7% by weight, respectively. The thicknesses of the coatings were 4.5μ, 4.7μ, and 4.6μ, respectively, and the co-stretchability was good. The oxygen permeability coefficient of the hollow body was approximately the same as that in Example 1.

実施例 4 i−プロピルアルコール70部と水30部とからな
る溶媒79部にエチレン含量率45モル%、ケン化度
99.5モル%のEVOH樹脂21部を加え75℃の温度下
に撹拌して溶解し透明な塗布液を調整した。実施
例1と同じパリソンの外表面をコロナ処理した
後、前記調整した60℃に保持した塗布液に浸漬し
て漬漬法で該パリソンの外表面にEVOH樹脂を
塗布した。塗布後、該被覆層の温度が55℃以上で
塗布液が発泡しない状態を保持していることを確
認しつつ、赤外線幅射による予備乾燥を行い、
105℃の熱風により乾燥した。該複合化された有
底パリソンの被覆内の揮発分は3.1重量%であり、
該樹脂の純量基準塗布量は、51g/m2であつた。
得られた該被覆層をもつ複合予備成形物を100℃
の温度に加熱し、二軸延伸吹込法により約1.5
の内容積をもつ二軸延伸された複合中空体を得
た。共延伸性は良好であつた。該中空体のポリエ
チレンテレフタレート樹脂部の温度が70℃以上に
ならないように注意しつつ、80℃の熱風で乾燥し
た後、該被覆を190℃数秒間熱処理した。該被覆
層の厚みは5.2μであつた。該中空体の酸素透過係
数は35℃、相対湿度45%の条件下で2.6×10-13
cm3・cm/cm2seccmHgであつた。
Example 4 79 parts of a solvent consisting of 70 parts of i-propyl alcohol and 30 parts of water with an ethylene content of 45 mol% and a degree of saponification
21 parts of 99.5 mol % EVOH resin was added and dissolved by stirring at a temperature of 75°C to prepare a transparent coating solution. After the outer surface of the same parison as in Example 1 was subjected to corona treatment, the EVOH resin was applied to the outer surface of the parison by immersion in the above-adjusted coating solution maintained at 60° C. by a dipping method. After coating, while making sure that the temperature of the coating layer is 55°C or higher and that the coating solution does not foam, pre-drying is carried out using infrared radiation.
It was dried with hot air at 105°C. The volatile content in the coating of the composite bottomed parison is 3.1% by weight,
The coating amount of the resin on a pure basis was 51 g/m 2 .
The resulting composite preform with the coating layer was heated at 100°C.
heated to a temperature of approximately 1.5 mm by biaxial stretching blowing method.
A biaxially stretched composite hollow body with an internal volume of . Co-stretchability was good. After drying with hot air at 80°C while being careful not to allow the temperature of the polyethylene terephthalate resin portion of the hollow body to exceed 70°C, the coating was heat-treated at 190°C for several seconds. The thickness of the coating layer was 5.2μ. The oxygen permeability coefficient of the hollow body is 2.6×10 -13 at 35℃ and 45% relative humidity.
cm 3 cm/cm 2 seccmHg.

実施例 5 実施例1および実施例4におけると同じ
EVOH樹脂の2種の塗布液を調整した。実施例
1と同じ有底パリソンに、先づ実施例4と同じ該
塗布液を実施例4と同様に浸漬法で塗布した。塗
布後、該第1被覆の再溶解を防ぐために赤外線幅
射(平均波長:2μ)による予備乾燥を行い、次
いで実施例1と同じ塗布液を、実施例1と同様に
第1被覆の上に浸漬法により塗布した。塗布後、
実施例1に準じ乾燥して、2層構造の被覆をもつ
複合化された有底パリソンを得た。該2層構造の
被覆の揮発分は2.8重量%であり、該樹脂の純量
基準塗布量は93g/m2であつた。得られた該複合
パリソンを実施例1に準じて二軸延伸吹込法で約
1.5の二軸延伸された複合中空体を得た後、乾
燥し、熱処理した。該2層構造の被覆の厚さは
9.4μであつた。該中空体の酸素透過係数は35℃相
対湿度45%の条件下で1.2×10-13cm3・cm/cm2・sec
cmHgであつた。共延伸性は良好であつた。
Example 5 Same as in Example 1 and Example 4
Two types of EVOH resin coating solutions were prepared. First, the same coating solution as in Example 4 was applied to the same bottomed parison as in Example 1 by the dipping method. After coating, preliminary drying was performed using infrared radiation (average wavelength: 2μ) to prevent re-dissolution of the first coating, and then the same coating solution as in Example 1 was applied onto the first coating in the same manner as in Example 1. It was applied by dipping method. After application,
It was dried in the same manner as in Example 1 to obtain a composite bottomed parison having a two-layered coating. The volatile content of the two-layer coating was 2.8% by weight, and the pure coating weight of the resin was 93 g/m 2 . The obtained composite parison was subjected to a biaxial stretching blowing method according to Example 1.
After obtaining a biaxially stretched composite hollow body of 1.5 mm, it was dried and heat treated. The thickness of the two-layer coating is
It was 9.4μ. The oxygen permeability coefficient of the hollow body is 1.2×10 -13 cm 3 cm/cm 2 cm 2 sec at 35°C and relative humidity 45%.
It was cmHg. Co-stretchability was good.

実施例 6 実施例1において用いた有底パリソンを用い
た。t−ブチルアルコール78部と水12部からなる
混合溶媒85部にエチレン含量55モル%、ケン化度
90モル%のEVOHを、15部を加え、80℃で撹拌
して透明な塗布液を調整した。先づ該パリソンに
前記調整した塗布液を実施例1に準じ浸漬法で塗
布した。(該塗布量を測定するために測定用サン
プルを乾燥して、塗布量を確認した。15g/m2
あつた。)該塗布後予備乾燥を赤外線幅射(平均
波長:2μ)で行つた後、実施例5と同様に実施
例1および実施例4におけると同じEVOH樹脂
の2種の塗布液を塗布し、部分乾燥し3層構造の
被覆をもつ複合パリソンを得た。該3層構造の被
覆の揮発分は4.5重量%であり、該樹脂の純量基
準塗布量は107g/m2であつた。得られた該複合
パリソンを実施例1に準じて二軸延伸−吹込法で
約1.5の二軸延伸された複合中空体を得た後乾
燥し、熱処理した。該3層構造の被覆の厚さは
10.6μであつた。該中空体の酸素透過係数は35℃、
相対湿度45%の条件下で0.95×10-13cm3・cm/
cm2・seccmHgであつた。
Example 6 The bottomed parison used in Example 1 was used. 85 parts of a mixed solvent consisting of 78 parts of t-butyl alcohol and 12 parts of water with an ethylene content of 55 mol% and a degree of saponification.
15 parts of 90 mol% EVOH was added and stirred at 80°C to prepare a transparent coating solution. First, the above-prepared coating solution was applied to the parison by the dipping method as in Example 1. (In order to measure the coating amount, the measurement sample was dried and the coating amount was confirmed. It was 15 g/ m2 .) After the coating, preliminary drying was performed using infrared radiation (average wavelength: 2 μ). Thereafter, in the same manner as in Example 5, two types of coating liquids of the same EVOH resin as in Examples 1 and 4 were applied and partially dried to obtain a composite parison having a three-layered coating. The volatile content of the three-layer coating was 4.5% by weight, and the pure coating amount of the resin was 107 g/m 2 . The obtained composite parison was subjected to a biaxial stretching/blowing method according to Example 1 to obtain a composite hollow body which was biaxially stretched to a diameter of about 1.5, and then dried and heat treated. The thickness of the three-layer coating is
It was 10.6μ. The oxygen permeability coefficient of the hollow body is 35℃,
0.95×10 -13 cm 3 cm/ under conditions of relative humidity 45%
It was cm2・seccmHg.

実施例 7 実施例6において、実施例1で用いたEVOH
樹脂溶液の塗布を行わず、2層構造の被覆をもつ
複合パリソンを実施例6に準じて得た。部分乾燥
後の該2層構造をもつ被覆層の揮発分は1.5重量
%であり、該樹脂の純量基準の塗布量は、65g/
m2であつた。得られた該複合パリソンを実施例1
に準じて二軸延伸−吹込法で約1.5の二軸延伸
された複合中空体を得た後乾燥し、熱処理した。
該2層構造の被覆の厚さは、6.6μであつた。該中
空体の酸素透過係数は35℃、相対湿度45%の条件
下で3.3×10-13cm3・cm/cm2seccmHgであつた。
Example 7 In Example 6, the EVOH used in Example 1
A composite parison having a two-layer coating was obtained according to Example 6 without applying the resin solution. The volatile content of the two-layered coating layer after partial drying is 1.5% by weight, and the coating amount based on the pure amount of the resin is 65g/
It was m2 . The obtained composite parison was prepared in Example 1.
A biaxially stretched composite hollow body of about 1.5 was obtained by a biaxially stretched blowing method according to the method, and then dried and heat treated.
The thickness of the two-layer coating was 6.6μ. The oxygen permeability coefficient of the hollow body was 3.3×10 -13 cm 3 ·cm/cm 2 seccmHg under the conditions of 35° C. and 45% relative humidity.

実施例 8 実施例2においてn−アミルアルコールに代え
てジメチルスルフオキシドをn−プロピルアルコ
ール/水混合溶媒に対し0.5重量%添加して行つ
た以外は、実施例2と同様に操作した。該被覆の
乾燥後の揮発分は、1.2重量%であつた。該複合
パリソンを二軸延伸−吹込に供した。共延伸性は
良好であり、得られた複合中空体の該被覆層の厚
みは8.5μであり、該中空体の酸素透過係数は、35
℃、相対湿度45%の条件下で1.2×10-13cm3・cm/
cm2・sec・cmHgであつた。
Example 8 The same procedure as in Example 2 was carried out, except that 0.5% by weight of dimethyl sulfoxide was added to the n-propyl alcohol/water mixed solvent instead of n-amyl alcohol. The volatile content of the coating after drying was 1.2% by weight. The composite parison was subjected to biaxial stretching and blowing. The co-stretchability was good, the thickness of the coating layer of the obtained composite hollow body was 8.5μ, and the oxygen permeability coefficient of the hollow body was 35.
1.2×10 -13 cm 3 cm/ under conditions of ℃ and 45% relative humidity.
It was cm2・sec・cmHg.

Claims (1)

【特許請求の範囲】 1 予備成形物の少くとも一つの壁面にエチレン
−酢酸ビニル共重合体ケン化物の溶剤溶液の被覆
を形成し、次いで該被覆中の揮発分が0.05〜5重
量%となるように乾燥したガス不透過性被覆をも
つ複合予備成形物。 2 被覆中の揮発分が0.1〜5重量%である特許
請求の範囲第1項記載の複合予備成形物。 3 溶剤が脂肪族アルコールと水の混合物であ
り、該揮発分が0.3〜5重量%である特許請求範
囲第1項記載の複合予備成形物。 4 溶剤がn−プロピルアルコール、i−プロピ
ルアルコール、t−ブチルアルコールまたはこれ
らのアルコールの2種以上の水の混合物である特
許請求の範囲第3項記載の複合予備成形物。 5 被覆中の揮発分が0.5〜5重量%である特許
請求の範囲第3項または第4項記載の複合予備成
形物。 6 予備成形物がポリエチレンテレフタレート系
樹脂からなる特許請求の範囲第1項ないし第5項
のいづれかに記載の複合予備成形物。 7 エチレン−酢酸ビニル共重合体ケン化物がエ
チレン含量25〜60モル%、ケン化度96モル%以上
である特許請求の範囲第1項ないし第6項のいづ
れかに記載の複合予備成形物。 8 被覆が(B)エチレン含量25〜35モル%、ケン化
度96モル%以上のエチレン−酢酸ビニル共重合体
ケン化物層と、(C)エチレン含量40〜60モル%、ケ
ン化度96モル%以上のエチレン−酢酸ビニル共重
合体ケン化物層の2層からなる特許請求の範囲第
1項ないし第6項のいづれかに記載の複合予備成
形物。 9 被覆が(A)エチレン含量25〜60モル%、ケン化
度85ないし95モル%のエチレン−酢酸ビニル共重
合体ケン化物層と、(B)エチレン含量25ないし35モ
ル%、ケン化度96モル%以上のエチレン−酢酸ビ
ニル共重合体ケン化物層および(C)エチレン含量40
ないし60モル%、ケン化度96モル%以上のエチレ
ン−酢酸ビニル共重合体ケン化物層からなり、最
内層が(A)である特許請求の範囲第1項ないし第6
項のいづれかに記載の複合予備成形物。 10 被覆がエチレン含量25ないし60モル%、ケ
ン化度96モル%以上のエチレン−酢酸ビニル共重
合体ケン化物層と(A)エチレン含量25ないし60モル
%、ケン化度85ないし95モル%のエチレン−酢酸
ビニル共重合体ケン化物層とからなり、内層が(A)
である特許請求の範囲第1項ないし第6項いづれ
かに記載の複合予備成形物。 11 予備成形物の少くとも一つの壁面にエチレ
ン−酢酸ビニル共重合体ケン化物の溶剤溶液の被
覆を形成し、次いで該被覆中の揮発分が0.05〜5
重量%となるように乾燥し、これを二軸延伸条件
下で二伸延伸−吹込成形したガス不透過性二軸延
伸複合中空体。 12 被覆中の揮発分が0.1〜5重量%である特
許請求の範囲第11項記載の複合中空体。 13 溶剤が脂肪族アルコールと水の混合物であ
り、該揮発分が0.3〜5重量%である特許請求範
囲第11項記載の複合中空体。 14 溶剤がn−プロピルアルコール、i−プロ
ピルアルコール、t−ブチルアルコールまたはこ
れらのアルコールの2種以上と水の混合物である
特許請求の範囲第13項記載の複合中空体。 15 被覆中の揮発分が0.5〜5重量%である特
許請求の範囲第13項または第14項記載の複合
中空体。 16 予備成形物がポリエチレンテレフタレート
系樹脂からなる特許請求の範囲第11項ないし第
15項のいづれかに記載の複合中空体。 17 エチレン−酢酸ビニル共重合体ケン化物が
エチレン含量25ないし60モル%、ケン化度96モル
%以上である特許請求の範囲第11項ないし第1
6項のいづれかに記載の複合中空体。 18 被覆が(B)エチレン含量25ないし35モル%、
ケン化度96モル%以上のエチレン−酢酸ビニル共
重合体ケン化物層と、(C)エチレン含量40ないし60
モル%、ケン化度96モル%以上のエチレン−酢酸
ビニル共重合体ケン化物層の2層からなる特許請
求の範囲第11項ないし第16項のいづれかに記
載の複合中空体。 19 被覆が(A)エチレン含量25ないし60モル%、
ケン化度85ないし95モル%のエチレン−酢酸ビニ
ル共重合体ケン化物層と(B)エチレン含量25ないし
35モル%、ケン化度96モル%以上のエチレン−酢
酸ビニル共重合体ケン化物層および(C)エチレン含
量40ないし60モル%、ケン化度96モル%以上のエ
チレン−酢酸ビニル共重合体ケン化物層からな
り、最内層が(A)である特許請求の範囲第11項な
いし第16項のいづれかに記載の複合中空体。 20 被覆がエチレン含量25ないし60モル%、ケ
ン化度96モル%以上のエチレン−酢酸ビニル共重
合体ケン化物層と(A)エチレン含量25ないし60モル
%、ケン化度85ないし95モル%のエチレン−酢酸
ビニル共重合体ケン化物層とからなり、内層が(A)
である特許請求の範囲第11項ないし第16項の
いづれかに記載の複合中空体。
[Claims] 1. A coating of a solvent solution of a saponified ethylene-vinyl acetate copolymer is formed on at least one wall of the preform, and then the volatile content in the coating is 0.05 to 5% by weight. Composite preform with a dry gas-impermeable coating. 2. The composite preform according to claim 1, wherein the volatile content in the coating is 0.1 to 5% by weight. 3. The composite preform according to claim 1, wherein the solvent is a mixture of aliphatic alcohol and water, and the volatile content is 0.3 to 5% by weight. 4. The composite preform according to claim 3, wherein the solvent is n-propyl alcohol, i-propyl alcohol, t-butyl alcohol, or a mixture of water of two or more of these alcohols. 5. The composite preform according to claim 3 or 4, wherein the volatile content in the coating is 0.5 to 5% by weight. 6. The composite preform according to any one of claims 1 to 5, wherein the preform is made of a polyethylene terephthalate resin. 7. The composite preform according to any one of claims 1 to 6, wherein the saponified ethylene-vinyl acetate copolymer has an ethylene content of 25 to 60 mol% and a saponification degree of 96 mol% or more. 8 The coating is (B) a saponified ethylene-vinyl acetate copolymer layer with an ethylene content of 25 to 35 mol% and a saponification degree of 96 mol% or more, and (C) an ethylene content of 40 to 60 mol% and a saponification degree of 96 mol % or more of saponified ethylene-vinyl acetate copolymer layers. 9 The coating comprises (A) a saponified ethylene-vinyl acetate copolymer layer having an ethylene content of 25 to 60 mol% and a saponification degree of 85 to 95 mol%, and (B) an ethylene content of 25 to 35 mol% and a saponification degree of 96. Saponified ethylene-vinyl acetate copolymer layer with mole% or more and (C) ethylene content 40
Claims 1 to 6 consist of a saponified ethylene-vinyl acetate copolymer layer with a saponification degree of 96 mol% or more and a saponification degree of 96 mol% or more, the innermost layer being (A).
Composite preform according to any of paragraphs. 10 The coating includes a saponified ethylene-vinyl acetate copolymer layer having an ethylene content of 25 to 60 mol% and a saponification degree of 96 mol% or more, and (A) a saponified ethylene-vinyl acetate copolymer layer having an ethylene content of 25 to 60 mol% and a saponification degree of 85 to 95 mol%. It consists of a saponified ethylene-vinyl acetate copolymer layer, and the inner layer is (A).
A composite preform according to any one of claims 1 to 6. 11 A coating of a solvent solution of a saponified ethylene-vinyl acetate copolymer is formed on at least one wall surface of the preform, and then the volatile content in the coating is 0.05 to 5.
A gas-impermeable biaxially stretched composite hollow body which is dried to a weight percentage and then bi-stretched and blow-molded under biaxially stretched conditions. 12. The composite hollow body according to claim 11, wherein the volatile content in the coating is 0.1 to 5% by weight. 13. The composite hollow body according to claim 11, wherein the solvent is a mixture of aliphatic alcohol and water, and the volatile content is 0.3 to 5% by weight. 14. The composite hollow body according to claim 13, wherein the solvent is n-propyl alcohol, i-propyl alcohol, t-butyl alcohol, or a mixture of two or more of these alcohols and water. 15. The composite hollow body according to claim 13 or 14, wherein the volatile content in the coating is 0.5 to 5% by weight. 16. The composite hollow body according to any one of claims 11 to 15, wherein the preform is made of a polyethylene terephthalate resin. 17 Claims 11 to 1, wherein the saponified ethylene-vinyl acetate copolymer has an ethylene content of 25 to 60 mol% and a saponification degree of 96 mol% or more.
The composite hollow body according to any one of Item 6. 18 The coating has (B) an ethylene content of 25 to 35 mol%,
A saponified ethylene-vinyl acetate copolymer layer with a saponification degree of 96 mol% or more, and (C) an ethylene content of 40 to 60
The composite hollow body according to any one of claims 11 to 16, comprising two saponified ethylene-vinyl acetate copolymer layers having a saponification degree of 96 mol% or more by mol%. 19 The coating has (A) an ethylene content of 25 to 60 mol%,
A saponified ethylene-vinyl acetate copolymer layer with a saponification degree of 85 to 95 mol% and (B) an ethylene content of 25 to 95 mol%.
A saponified ethylene-vinyl acetate copolymer layer with an ethylene content of 35 mol% and a saponification degree of 96 mol% or more, and (C) an ethylene-vinyl acetate copolymer layer with an ethylene content of 40 to 60 mol% and a saponification degree of 96 mol% or more. The composite hollow body according to any one of claims 11 to 16, which is made of a compound layer, and the innermost layer is (A). 20 The coating has a saponified ethylene-vinyl acetate copolymer layer with an ethylene content of 25 to 60 mol% and a saponification degree of 96 mol% or more, and (A) an ethylene content of 25 to 60 mol% and a saponification degree of 85 to 95 mol%. It consists of a saponified ethylene-vinyl acetate copolymer layer, and the inner layer is (A).
A composite hollow body according to any one of claims 11 to 16.
JP11253283A 1983-06-21 1983-06-21 Spare shape with gas impermeable coating and biaxial oriented composite hollow body Granted JPS602361A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11253283A JPS602361A (en) 1983-06-21 1983-06-21 Spare shape with gas impermeable coating and biaxial oriented composite hollow body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11253283A JPS602361A (en) 1983-06-21 1983-06-21 Spare shape with gas impermeable coating and biaxial oriented composite hollow body

Publications (2)

Publication Number Publication Date
JPS602361A JPS602361A (en) 1985-01-08
JPH0356168B2 true JPH0356168B2 (en) 1991-08-27

Family

ID=14588996

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11253283A Granted JPS602361A (en) 1983-06-21 1983-06-21 Spare shape with gas impermeable coating and biaxial oriented composite hollow body

Country Status (1)

Country Link
JP (1) JPS602361A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61243833A (en) * 1985-04-19 1986-10-30 Nippon Synthetic Chem Ind Co Ltd:The Production of polyester molding of excellent gas barrier property
JPH0677717B2 (en) * 1989-02-27 1994-10-05 日本合成化学工業株式会社 Method for forming coating film of saponified ethylene-vinyl acetate copolymer
FR2653756B1 (en) * 1989-10-31 1992-05-15 Ono MULTILAYER STRUCTURE FOR PACKAGING OXYGEN SENSITIVE PRODUCTS.
KR100312673B1 (en) * 1998-09-28 2001-11-03 나카무라 하사오 Multilayered film

Also Published As

Publication number Publication date
JPS602361A (en) 1985-01-08

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