JPS60124661A - Method for forming coating film of saponified ethylene/ vinyl acetate copolymer - Google Patents
Method for forming coating film of saponified ethylene/ vinyl acetate copolymerInfo
- Publication number
- JPS60124661A JPS60124661A JP23326583A JP23326583A JPS60124661A JP S60124661 A JPS60124661 A JP S60124661A JP 23326583 A JP23326583 A JP 23326583A JP 23326583 A JP23326583 A JP 23326583A JP S60124661 A JPS60124661 A JP S60124661A
- Authority
- JP
- Japan
- Prior art keywords
- vinyl acetate
- acetate copolymer
- coating film
- weight
- saponified
- 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
Links
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- Compositions Of Macromolecular Compounds (AREA)
- Paints Or Removers (AREA)
Abstract
Description
【発明の詳細な説明】
エチレン含量25〜55モル%、酢酸ビニル成分のケン
化度90モル%以上のエチレン−酢酸ビニル共重合体ケ
ン化物から得?、れる皮膜は透明性、酸素遮断性等にす
ぐれ、食品、医療品、工業薬品等の各種包装材としであ
るいはプラスチックフィルム、紙、金属箔等とラミネー
トした複合材料として有用である。DETAILED DESCRIPTION OF THE INVENTION Obtained from a saponified ethylene-vinyl acetate copolymer having an ethylene content of 25 to 55 mol% and a degree of saponification of the vinyl acetate component of 90 mol% or more. The resulting film has excellent transparency and oxygen barrier properties, and is useful as a variety of packaging materials for foods, medical products, industrial chemicals, etc., or as a composite material laminated with plastic film, paper, metal foil, etc.
しかして、該ケン化物の皮膜を形成させる場合、任意の
方法が実施可能であるが、比較的膜厚の薄い皮膜が形成
で終る点、中空容器等の複雑な形の基材に対しても容易
に皮膜の形成ができる点、及び比較的簡単な装置で塗工
操作ができる点で該ケン化物を溶剤に溶解した溶液を基
材に塗布する溶液コーティング法が注目されている。When forming a film of the saponified product, any method can be used, but it ends up forming a relatively thin film, and it is not suitable for substrates with complex shapes such as hollow containers. A solution coating method, in which a solution of the saponified product dissolved in a solvent is applied to a substrate, is attracting attention because a film can be easily formed and the coating operation can be performed using relatively simple equipment.
かかる方法において該ケン化物の溶剤としてこれまでに
多数のものが提案されているが例えば特公昭46−23
911号公報や特公昭47−48489号公報に記載さ
れる含水プロピルアルコールや含水ブチルアルコールが
透明な皮膜が得C2れるという点で有望視されている。In this method, many solvents have been proposed for the saponified product, for example, Japanese Patent Publication No. 46-23
Water-containing propyl alcohol and water-containing butyl alcohol described in Japanese Patent Publication No. 911 and Japanese Patent Publication No. 47-48489 are considered to be promising in that they produce transparent films.
しかしながら、本発明者等が検討したところ、かかる含
水アルコール系での塗膜形成の場合、塗液を50℃とい
う高温に保持して塗布操作を行なわなければ透明性の良
い塗膜が得られない難点や塗液の貯薫安定性や放置安定
1つが悪く、使用時に高温で再溶解する必要がある等の
欠点があることが?!明した。かかる高温の保持は余分
の熱エネルギーが必要となる上、溶媒の蒸発に伴なう塗
液の濃度変化をもたらすので塗布操作を密閉系で実施せ
ざるを得ない等の工程管理面で解決すべき問題点となる
。更に塗膜の透明性やガス遮断性等の塗膜物性面におい
てもミクロ的に均質な塗膜を形成しがたいという理由か
ら近時の厳しい品質要求に必ずしも充分対処できるとは
言いがたく、更に一層塗膜物性の向上が必要とされるの
である。However, the present inventors have investigated and found that when forming a coating film using such a hydroalcoholic system, a coating film with good transparency cannot be obtained unless the coating solution is maintained at a high temperature of 50°C and the coating operation is performed. Disadvantages: The storage stability and storage stability of the coating liquid are poor, and there are disadvantages such as the need to re-dissolve at high temperature when using it. ! I made it clear. Maintaining such a high temperature not only requires extra thermal energy, but also causes changes in the concentration of the coating solution due to evaporation of the solvent, which can be solved in terms of process control, such as having to perform the coating operation in a closed system. This is a problem that should be addressed. Furthermore, it is difficult to form a microscopically homogeneous coating film in terms of coating film properties such as transparency and gas barrier properties, so it cannot be said that it is necessarily sufficient to meet the recent strict quality requirements. There is a need to further improve the physical properties of the coating film.
しかるに本発明者等はかかる問題を解決すべ(鋭意研究
を重ねた結果、エチレン含125〜55モル%、酢酸ビ
ニル成分のケン化度90モル%以上のエチレン−酢酸ビ
ニル共重合体ケン化物の溶液を基材に塗布、乾燥して該
ケン化物の塗膜を形成するに当たり、溶剤として(A)
水 10〜60重量%
(B) プロピルアルコール、ブチルアルコール又はベ
ンジルアルコールの少ft< )−tr 1135〜7
0重量%
(’C) 蟻酸 2〜85重量%
からなる混合物を使用する場合、目的が達成できること
を見出し本発明を完成するに到った。However, the present inventors have attempted to solve this problem (as a result of extensive research, we have developed a solution of a saponified ethylene-vinyl acetate copolymer with an ethylene content of 125 to 55 mol% and a degree of saponification of the vinyl acetate component of 90 mol% or more). (A) as a solvent when coating on a base material and drying to form a coating film of the saponified product.
Water 10-60% by weight (B) Small amount of propyl alcohol, butyl alcohol or benzyl alcohol ft< )-tr 1135-7
The present invention was completed based on the finding that the object can be achieved when a mixture consisting of 0% by weight ('C) formic acid and 2 to 85% by weight is used.
本発明ではかかる特定の混合溶媒を用いる場合、常温で
塗布操作を行なっても常に安定して透明性やガス遮断性
が着しく向上した塗膜が得られるので、塗布操作時に特
別な管理が不必要となり、従来法の欠点が解消できる点
でその産業上の有用性は極めて大である。In the present invention, when such a specific mixed solvent is used, a stable coating film with improved transparency and gas barrier properties is always obtained even when the coating operation is performed at room temperature, so no special management is required during the coating operation. Its industrial usefulness is extremely great in that it is necessary and the drawbacks of the conventional method can be overcome.
本発明で用いるエチレン−酢酸ビニル共重合体ケン化物
は、エチレン含量25〜55モル%好ましくは28〜4
8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%以上でなければならない。エチ
レン含量が25モル%以下では高温時のガス遮断性が低
下し、一方55モル%稗上では充分なガス遮断性や印刷
適性等の塗膜物性等が劣化する。又、ケン化度が90モ
ル%以下でけガス遮断性や耐湿性が低下する。The saponified ethylene-vinyl acetate copolymer used in the present invention has an ethylene content of 25 to 55 mol%, preferably 28 to 4 mol%.
The degree of saponification of the vinyl acetate component should be 90 mol% or more, preferably 95 mol% or more. If the ethylene content is less than 25 mol %, the gas barrier property at high temperatures will decrease, while if it is above 55 mol %, the physical properties of the coating film, such as sufficient gas barrier property and printability, will deteriorate. Further, when the degree of saponification is 90 mol% or less, gas barrier properties and moisture resistance decrease.
又該共重合体ケン化物は更に少量のプロピレン、イソブ
チン、a−オクテン、a−ドデセン、a−オクタデセン
等の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中ニトリ
ル・アミド・無水物、不飽和スルホン酸又はその塩等の
コモ7マーを含んでいても差支えない。The saponified copolymer further contains a small amount of α-olefin such as propylene, isobutyne, a-octene, a-dodecene, and a-octadecene, an unsaturated carboxylic acid or a salt thereof,
Partial alkyl esters and complete alkyl esters may contain co-7mers such as nitriles, amides, anhydrides, unsaturated sulfonic acids, or salts thereof.
本発明においては、上記ケン化物の溶媒として(A)水
10〜60fii1%、(B)7’ロビルアルコール、
ブチルアルコール又はベンノルアルコールの少なくとも
1種5〜70重量%、CC’)m酸2〜85重量%から
なる混合物を使用するもので、従来用いられている水/
プロピルアルコールあるいは水/ブチルアルコール溶媒
の前記欠点を特定量の蟻酸を配合することによって解決
するものである。In the present invention, as the solvent for the saponified product, (A) water 10 to 60fii1%, (B) 7' lobil alcohol,
It uses a mixture consisting of 5 to 70% by weight of at least one of butyl alcohol or bennor alcohol and 2 to 85% by weight of CC')m acid.
The above-mentioned drawbacks of propyl alcohol or water/butyl alcohol solvents are solved by incorporating a specific amount of formic acid.
蟻酸あるいは含水蟻酸もエチレン−酢酸ビニル共重合体
ケン化物の溶媒として公知であるが、本発明者等の検討
では単にエチレン−酢酸ビニル共重合体ケン化物の溶ル
との組み介オ)せにおいて蟻酸は各種の溶媒の中でも特
異な性能を有するものと考えられ、本願の効果は公知事
曲記混合溶媒において(A)水の含量は10〜60重量
%、好ましくは30〜50重量%でなければならない。Formic acid or hydrated formic acid is also known as a solvent for saponified ethylene-vinyl acetate copolymer, but the present inventors' studies have shown that it is possible to use formic acid simply in combination with a solution of saponified ethylene-vinyl acetate copolymer. Formic acid is considered to have unique performance among various solvents, and the effect of the present application is that (A) the water content in the publicly known mixed solvent must be 10 to 60% by weight, preferably 30 to 50% by weight. Must be.
10重量%以下では均一な溶液が得難く、60重量%以
上ではケン化物の溶解性が着しく低下するという問題点
が生じる。又、(B)のプロピルアルコール、ブチルア
ルコール、ベンノルアルコールは5〜70重量%、好ま
しくは40〜60重量%の含有量でなければならない、
5重皿%以下ではかなり多量の蟻酸を使用しなければ溶
解性が低下するという難点があり、70重量%以上では
均一な溶液が得難く、実用性に乏しい、更に(C)Il
酸の含有量は2〜85重量%、好ましくは5〜40重量
%、特に好ましくは10〜30重量%でなければならな
い、2重量%以下では本発明の効果に乏しく、その添加
効果が認めがたい、85重量%以上の蟻酸の使用は装置
の腐食という点で好ましくない、(B)成分のプロピル
アルコールとしてはn−プロピルアルコール、1so−
プロピルアルコールが、又ブチルアルコールとしてはn
−ブチルアルコール、1so−ブチルアルコール、5e
C−ブチルアルコール、tert−ブチルアルコール等
が挙げられるが、1so−プロピルアルコールが好適に
使用される。(B)以外のアルコールに蟻酸を添加して
も透明性の良好な塗膜を得ることは出来ない。If it is less than 10% by weight, it is difficult to obtain a uniform solution, and if it is more than 60% by weight, the problem arises that the solubility of the saponified product is severely reduced. In addition, the content of propyl alcohol, butyl alcohol, and benol alcohol in (B) must be 5 to 70% by weight, preferably 40 to 60% by weight.
If it is less than 5% by weight, the solubility will decrease unless a large amount of formic acid is used, and if it is more than 70% by weight, it will be difficult to obtain a homogeneous solution and it will be impractical, and (C)Il
The content of acid must be 2 to 85% by weight, preferably 5 to 40% by weight, particularly preferably 10 to 30% by weight. If it is less than 2% by weight, the effect of the present invention will be poor and the effect of its addition will not be recognized. However, the use of formic acid of 85% by weight or more is not preferable in terms of corrosion of the equipment.As the propyl alcohol of component (B), n-propyl alcohol, 1so-
Propyl alcohol is also n as butyl alcohol.
-butyl alcohol, 1so-butyl alcohol, 5e
Examples include C-butyl alcohol, tert-butyl alcohol, and 1so-propyl alcohol is preferably used. Even if formic acid is added to alcohols other than (B), a coating film with good transparency cannot be obtained.
又(C)において蟻酸は、メチルエステル、エチルエス
テル、プロピルエステル等の任意のアルキルエステル類
であっても本願の効果は同様に得られる。Further, in (C), formic acid may be any alkyl ester such as methyl ester, ethyl ester, propyl ester, etc., and the same effect of the present invention can be obtained.
エチレン−酢酸ビニル共重合体ケン化物溶液の濃度は特
に制限はなく任意の範囲で塗工可能であるが、通常は0
.5〜+ 5 、m 量%程度が好ましい。本発明では
濃度が低し・塗液の場合であっても、塗膜の白濁がおこ
らな〜1ことも特徴点の一つであり、含水アルコールを
溶媒とする従来法における塗液塗布の場合比較的高濃度
の溶液が使用され、その結果塗膜厚の調整に煩わしさが
避けられな(・ことを考慮するとかかる点でも本発明の
優位性は大である。The concentration of the saponified ethylene-vinyl acetate copolymer solution is not particularly limited and can be coated within any range, but it is usually 0.
.. The amount is preferably about 5 to +5, m%. One of the features of the present invention is that even if the concentration is low and the coating liquid is used, the coating film will not become cloudy. A relatively highly concentrated solution is used, and as a result, the adjustment of the coating film thickness is unavoidably troublesome. Considering this, the present invention has great advantages in this respect as well.
本発明の効果が特に顕著に発揮されるのは低a1度即ち
3〜10重鼠%程度の塗液を用いる場合である。しかも
]二記塗液は安定性にすぐれるため、特に加熱等の特別
な操作をしなくてもケン化物の沈澱が析出したりする心
配は全(ない−ヒ、低温での溶液の貯蔵安定性もすぐれ
でいるので、塗膜形成は常温程度の温度で任意に実施可
能である。The effects of the present invention are particularly pronounced when a coating liquid with a low a1 degree, that is, about 3 to 10% by weight, is used. Moreover, since the coating liquid mentioned above has excellent stability, there is no need to worry about precipitation of saponified substances even without special operations such as heating. Since it has excellent properties, coating film formation can be carried out at any temperature around room temperature.
本発明においてエチレン−酢酸ビニル共重合体ケン化物
が塗布される基材としては特に制限はなく、ポリエチレ
ン、ポリプロピレン、ポリエステル、ポリスチレン、ポ
リ塩化ビニル等の各種プラスチックスのフィルム、シー
ト、中空容器あるいは紙、セロファン、セルローズアセ
テート、天然ゴム、合成ゴム、金属等が挙げられる。In the present invention, the substrate to which the saponified ethylene-vinyl acetate copolymer is applied is not particularly limited, and includes films, sheets, hollow containers, and paper made of various plastics such as polyethylene, polypropylene, polyester, polystyrene, and polyvinyl chloride. , cellophane, cellulose acetate, natural rubber, synthetic rubber, metal, etc.
かかる是材の膜厚はlO〜1000μ程度が適当である
。本発明ではかかる基材にエチレン−酢酸ビニル共重合
体ケン化物を塗布して得られる積層物の形状でそのまま
包装材料として実用化されるのが普通であるが、必要で
あればかかる基材からエチレン−酢酸ビニル共重合体ケ
ン化物の塗膜を剥離して単層フィルム、シート等として
も使用可能である。The film thickness of such a material is suitably about 10 to 1000 microns. In the present invention, the laminate obtained by applying a saponified ethylene-vinyl acetate copolymer to such a base material is usually put to practical use as a packaging material as it is, but if necessary, such a base material can be used. The saponified ethylene-vinyl acetate copolymer can also be used as a single-layer film, sheet, etc. by peeling off the coating.
塗布の方法としてはローラーコーティング法、スプレー
コーティング法、ディップコーティング法その他任意の
公知方法が適用できる。As a coating method, any known method such as a roller coating method, a spray coating method, a dip coating method or the like can be applied.
又、基材の種類によってはエチレン−酢酸ビニル共重合
体ケン化物層との接着力を向上させるため、表面酸化処
理、火炎処理、アンカーコート処理、プライマー処理等
が適宜実施可能である。Further, depending on the type of the base material, surface oxidation treatment, flame treatment, anchor coating treatment, primer treatment, etc. can be carried out as appropriate in order to improve the adhesive force with the saponified ethylene-vinyl acetate copolymer layer.
アンカー処理剤としてはポリウレタン系化合物やポリエ
ステル・イソシアj−ト系化合物が好適に利用され得る
。アンカーフート層の膜厚は0.05〜3μ程度が実用
的である。As the anchor treatment agent, polyurethane compounds and polyester isocyanate compounds can be suitably used. The practical thickness of the anchor foot layer is about 0.05 to 3 μm.
エチレン−酢酸ビニル共重合体ケン化物の溶液を基材に
塗布した後、乾燥が行なわれる。乾燥温度は30〜15
0℃好ましくは50〜120℃程度の温度で3秒〜5分
程度加熱すれば良い、かかる乾燥にお(1て塗膜中の揮
発分、即ち水、アルコール及び蟻酸が除去されるのであ
ろ力C1水や@酸はかなり沸点が高いにもかかわらず、
共存するアルコール類が蟻酸や水の蒸発を促進するもの
と思われ、上記程度の乾燥温度で充分である。塗膜の乾
燥は揮発分がほとんどな(なるまで打なうことも出来る
が、塗膜にり2ンキングが発生するのを防止したり、塗
膜の透明性や層間接着力を長期間にわたって維持するこ
とが出来る様に揮発分を塗膜中に0.5〜10重量%残
存させるのが有利である。揮発分のうちでも水を0.3
〜9重量%、アルコールを0〜0.5重量%、蟻酸を0
〜1.5重量%の割合となる桶、塗液の組成や乾燥条件
を設定するのが望ましい。After applying a solution of saponified ethylene-vinyl acetate copolymer to a substrate, drying is performed. Drying temperature is 30-15
Heating at a temperature of 0°C, preferably 50 to 120°C, for about 3 seconds to 5 minutes is enough. Despite the fact that C1 water and @acids have fairly high boiling points,
It is thought that the coexisting alcohols promote the evaporation of formic acid and water, and the above-mentioned drying temperature is sufficient. The drying of the paint film can be done until most of the volatile matter is removed (although it is possible to dry the paint film until the volatile matter is almost completely removed), it is necessary to prevent the occurrence of 2-inking in the paint film and to maintain the transparency and interlayer adhesion of the paint film for a long period of time. It is advantageous to leave 0.5 to 10% by weight of volatile matter in the coating film so that water can be retained at 0.3% by weight.
~9% by weight, 0-0.5% by weight of alcohol, 0% of formic acid
It is desirable to set the composition of the tub, coating liquid, and drying conditions so that the ratio is 1.5% by weight.
かくしてエチレン−酢酸ビニル共重合体ケン化物の透明
な塗膜が形成されるわけであるが、その膜厚は0.5〜
10μ程度が実用的である。0.5μ以下では充分なガ
ス遮断性が発揮し難(、一方10μ以上の膜厚ぐはその
コントロールに困難を生じる。又必要に応じて該塗膜上
に更に塩化ビニリデン樹脂コート、塩化ビニル−酢酸ビ
ニル共重合体ニーF等によって防湿層を形成させること
も勿論可能である。得られる塗膜はエチレン−酢酸ビニ
ル共重合体ケン化物の単層フィルム、シートはもとより
ポリエステル、ポリオレフィン等にラミネートした複合
材料として食品、飲料、薬品、医薬等の包装材料あるい
は容器として有用である。実用性が高い包装材料、容器
の層構成としては代表的には膜厚10〜1000μの基
材(ポリエステル、ポリエチレン等)/IR厚0.05
〜3μのアンカーニー)Jl/膜厚0.5〜10μのエ
チレン−酢酸ビニル共重合体ケン化物(揮発分合fi0
.5〜5重量%)あるいは上記の構造のエチレン−酢酸
ビニル共重合体ケン化物層の上に更twig厚0.5〜
3μ程度の塩化ビニリデン0j脂層、ある(1は塩化ビ
ニル−酢酸ビニル共重合体層を設けたものである。In this way, a transparent coating film of the saponified ethylene-vinyl acetate copolymer is formed, and the film thickness is 0.5~
A thickness of about 10μ is practical. If it is less than 0.5μ, it will be difficult to exhibit sufficient gas barrier properties (on the other hand, if the film thickness is more than 10μ, it will be difficult to control it.If necessary, the coating film may be further coated with vinylidene chloride resin, vinylidene chloride resin, etc.). Of course, it is also possible to form a moisture-proof layer with vinyl acetate copolymer Ni-F, etc. The resulting coating film can be a single-layer film or sheet of saponified ethylene-vinyl acetate copolymer, or it can be laminated onto polyester, polyolefin, etc. As a composite material, it is useful as a packaging material or container for foods, beverages, drugs, pharmaceuticals, etc.The layer structure of highly practical packaging materials and containers is typically a base material with a film thickness of 10 to 1000μ (polyester, polyethylene etc.)/IR thickness 0.05
~3μ anchor knee) Jl/film thickness 0.5~10μ saponified ethylene-vinyl acetate copolymer (volatile fraction fi0
.. 5 to 5% by weight) or on top of the saponified ethylene-vinyl acetate copolymer layer with the above structure, an additional twig thickness of 0.5 to 5% by weight)
There is a vinylidene chloride 0j fat layer of about 3μ (1 is the one provided with a vinyl chloride-vinyl acetate copolymer layer).
その形状はフィルム状、シート状、中空ビン、チューブ
等任意のものであって良い。Its shape may be arbitrary, such as a film, a sheet, a hollow bottle, or a tube.
以下、実例を挙げて本発明の方法を更に詳しく説明する
5%、部とあるのli特にことわりのない限り、いずれ
も重量基準である。Hereinafter, the method of the present invention will be explained in more detail with reference to examples. Unless otherwise specified, 5%, parts, and li are based on weight.
実例1
水30%、1so−プロピルアルコール50%、蟻酸2
0%を含む混合溶媒95部とエチレン−酢酸ビニル共重
合体ケン化物(エチレン含′136モル%、ケン化度9
9.5モル%)59を加え40〜50℃にて約1時間攪
拌し透明な溶液を調製した。 一方膜厚50μのポリエ
チレンテレフタレート製のフィルムにポリウレタン系接
着剤主剤100部、硬化剤6.5部、酢酸エチル900
部からなるポリウレタン系化合物溶液を用いて膜lv3
μのアンカーフート処理を施した。Example 1 Water 30%, 1so-propyl alcohol 50%, formic acid 2
95 parts of a mixed solvent containing
9.5 mol %) 59 was added and stirred at 40 to 50°C for about 1 hour to prepare a transparent solution. On the other hand, on a polyethylene terephthalate film with a film thickness of 50 μm, 100 parts of a polyurethane adhesive base agent, 6.5 parts of a hardening agent, and 900 parts of ethyl acetate were added.
Membrane lv3 using a polyurethane compound solution consisting of
μ anchor foot treatment was applied.
この様に処理したフィルムを液温25℃の前記塗液に浸
潰し、直ちに70℃にて2分乾燥を行ない、水分含量1
.3%、1so−プロピルアルコール含fio、 1%
、蟻酸fjlo、、2%のエチレン−酢酸ビニル共重合
体ケン化物(I11厚5μ)の塗膜を形成させた。The film treated in this way was immersed in the coating solution at a temperature of 25°C, and immediately dried at 70°C for 2 minutes to reduce the water content to 1.
.. 3%, fio containing 1so-propyl alcohol, 1%
, formic acid fjlo, and a 2% saponified ethylene-vinyl acetate copolymer copolymer (I11 thickness 5 μm) coating film was formed.
該#t171iI物の透明性を^STM 01003−
52に従って測定したところ、ヘイズ値は13%で極め
て良好な透明性を示した。The transparency of the #t171iI product is ^STM 01003-
52, the haze value was 13%, indicating very good transparency.
(基材のヘイズ値は14%)
又、酸素遮断性を^STN 01434−58に従って
測定したところ、酸素透過率は7 cc(NTP)/−
2・241+r ・at−であり、良好な〃ス遮断性を
示した。(The haze value of the base material is 14%) Also, when the oxygen barrier property was measured according to ^STN 01434-58, the oxygen permeability was 7 cc (NTP)/-
2.241+r.at-, showing good gas-blocking properties.
更に層間接着強度を測定したところ、いずれの層間接着
力も300g/25am以上で極めて良好でありた。Furthermore, when the interlayer adhesion strength was measured, all interlayer adhesion strengths were 300 g/25 am or more, which was extremely good.
又、上記積層物を65%R11,20’Cの雰囲気下に
1o日間放置してもクラッキング等の発生や透明性の低
下は認められず、外観、層間接着力はほとんど不変であ
った。Further, even when the above laminate was left in an atmosphere of 65% R11,20'C for 10 days, no cracking or decrease in transparency was observed, and the appearance and interlayer adhesion remained almost unchanged.
幻照例1
実例1において蟻酸の使用を省略した以外は同例と同一
の実験を行なったところ、ヘイズ値は85%、酸素透過
率は45cc(旧’P )7m2・241+r ・al
mにいずれも低下した。塗工時の液温を60℃まで上昇
させたところ、上記ヘイズ値は55%、酸素透過率は4
0cc(NTP)/+s2・24hr−atmであっ対
照例2,3
蟻酸に代えてエチレンジアミンを用いた(対照例2)、
及び1so−プロピルアルコールに代えでエチルアルコ
ールを用いた(対照例3)以外は同例に準じて実験を行
なった。ヘイズ値は対照例2が80%、対照例3が31
5%であり、酸素透過率は対照例2が41cc(NTP
)7m2・24br−at+s、対照例3が43cc(
NTP)/+s’ ・24hr−ata+に過ぎなかっ
た。Illusion Example 1 When the same experiment as Example 1 was conducted except that the use of formic acid was omitted, the haze value was 85% and the oxygen permeability was 45cc (formerly 'P) 7m2・241+r・al
Both values decreased to m. When the liquid temperature during coating was raised to 60°C, the haze value was 55% and the oxygen permeability was 4.
0cc(NTP)/+s2・24hr-atm Control Examples 2 and 3 Ethylenediamine was used instead of formic acid (Control Example 2),
An experiment was conducted according to the same procedure except that ethyl alcohol was used instead of 1so-propyl alcohol (Control Example 3). The haze value is 80% for control example 2 and 31 for control example 3.
5%, and the oxygen permeability of control example 2 was 41cc (NTP
) 7m2・24br-at+s, control example 3 was 43cc (
NTP)/+s' ・24hr-ata+.
実例2〜81対照例4〜9
第1表及び第2表に示す如き条件下で実例1に準じて塗
膜形成を行なった。その結果を第1表、第2表に示す。Examples 2 to 81 Comparative Examples 4 to 9 Coating films were formed according to Example 1 under the conditions shown in Tables 1 and 2. The results are shown in Tables 1 and 2.
但し、実例7.8においてはエチレン−酢酸ビニル共重
合体ケン化物層上に更に膜厚2μの塩化ビニリデン儲1
脂層、及び塩化ビニル−酢酸ビニル共重合体層をそれぞ
れ設けたものである。However, in Example 7.8, a layer of vinylidene chloride with a thickness of 2μ was added on the saponified ethylene-vinyl acetate copolymer layer.
A fat layer and a vinyl chloride-vinyl acetate copolymer layer are respectively provided.
尚、各基材の酸素透過率(cc(NTP)/m’ ・2
41+r−atm )は次の通りである。In addition, the oxygen permeability of each base material (cc (NTP)/m' ・2
41+r-atm) is as follows.
Claims (1)
ケン化度90モル%以上のエチレン−酢酸ビニル共重合
体ケン化物の溶液を基材に塗布、乾燥して該ケン化物の
塗膜を形成するに当たり、溶剤として (A) 水 10〜60重1% (B) プロピルアルコール、ブチルアルコール又はベ
ンシルアルコールの少な(とも1種 5〜70重量% (C)@酸 2=85重量% からなる混合物を使用することを特徴とするエチレン−
酢酸ビニル共重合体ケン化物の塗膜形成方法。 2、ポリウレタン系化合物でアンカーコートされた基材
を使用することを特徴とする特許請求の範囲第1項記載
の方法。 3、膜厚10〜1000μの基材/膜厚0.05〜3μ
のアンカーコート層からなる積層物に膜厚0.5〜10
μのエチレン−酢酸ビニル共重合体クン化物塗膜を形成
させることを特徴とする特Fr1ll求の範囲第2項記
載の方法。 4、エチレン−酢酸ビニル共重合体ケン化物の塗膜中の
揮発分を0.5〜1031量%とすることを特徴とする
特許請求の@H第3項記載の方法。 5、エチレン−酢酸ビニル共重合体ケン化物の溶液とし
て樹脂濃度0.5〜15重量%の溶液を使用することを
特徴とする特許請求の範囲第1〜4項記載の方法。 6、エチレン−酢酸ビニル共重合体ケン化物の溶液を基
材に塗布した後、30〜150℃、3秒〜5分の条件下
に乾燥を行なうことを特徴とする特許請求の範囲第1〜
4項記載の方法。[Scope of Claims] 1. A solution of a saponified ethylene-vinyl acetate copolymer having an ethylene content of 25 to 55 mol% and a degree of saponification of vinyl acetate component of 90 mol% or more is applied to a base material and dried. In forming a coating film of the compound, as a solvent (A) water 10-60% by weight (B) a small amount of propyl alcohol, butyl alcohol or benzyl alcohol (5-70% by weight of each type) (C) @acid 2 =85% by weight of ethylene-
Method for forming a coating film of saponified vinyl acetate copolymer. 2. The method according to claim 1, characterized in that a substrate anchor-coated with a polyurethane compound is used. 3. Base material with film thickness 10-1000μ/film thickness 0.05-3μ
A laminate consisting of an anchor coat layer with a film thickness of 0.5 to 10
2. The method according to item 2, characterized in that a coating film of a cyanide of ethylene-vinyl acetate copolymer of μ is formed. 4. The method according to claim 3, characterized in that the volatile content in the coating film of the saponified ethylene-vinyl acetate copolymer is 0.5 to 1031% by weight. 5. The method according to claims 1 to 4, characterized in that a solution having a resin concentration of 0.5 to 15% by weight is used as the solution of the saponified ethylene-vinyl acetate copolymer. 6. Claims 1 to 6, characterized in that after applying a solution of saponified ethylene-vinyl acetate copolymer to a substrate, drying is performed at 30 to 150°C for 3 seconds to 5 minutes.
The method described in Section 4.
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23326583A JPS60124661A (en) | 1983-12-09 | 1983-12-09 | Method for forming coating film of saponified ethylene/ vinyl acetate copolymer |
CA000446736A CA1251103A (en) | 1983-12-09 | 1984-02-03 | Process for forming film of hydrolysed ethylene-vinyl acetate copolymer |
GB08403322A GB2150934B (en) | 1983-12-09 | 1984-02-08 | Process for forming film of hydrolysed ethylene-vinyl acetate copolymer |
DE19843404425 DE3404425A1 (en) | 1983-12-09 | 1984-02-08 | METHOD FOR FORMING A FILM FROM A HYDROLYSED ETHYLENE / VINYL ACETATE COPOLYMER |
FR8401943A FR2556357B1 (en) | 1983-12-09 | 1984-02-08 | PROCESS FOR FORMING A FILM OF A HYDROLYZED VINYL ETHYLENE ACETATE COPOLYMER |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23326583A JPS60124661A (en) | 1983-12-09 | 1983-12-09 | Method for forming coating film of saponified ethylene/ vinyl acetate copolymer |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60124661A true JPS60124661A (en) | 1985-07-03 |
Family
ID=16952371
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP23326583A Pending JPS60124661A (en) | 1983-12-09 | 1983-12-09 | Method for forming coating film of saponified ethylene/ vinyl acetate copolymer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60124661A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1992014785A1 (en) * | 1991-02-15 | 1992-09-03 | Kuraray Co., Ltd. | Aqueous dispersion and base material coated therewith |
US5542986A (en) * | 1991-01-30 | 1996-08-06 | Elf Atochem North America, Inc. | Paint strippers process |
US5726140A (en) * | 1992-06-02 | 1998-03-10 | Elf Atochem North America, Inc. | Water-in-oil emulsion having aqueous phase evaporation retarded with wax |
US5780409A (en) * | 1992-06-02 | 1998-07-14 | Elf Atochem North America, Inc. | Water-in-oil emulsion having aqueous phase evaporation retarded with wax IR 3323D |
-
1983
- 1983-12-09 JP JP23326583A patent/JPS60124661A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5542986A (en) * | 1991-01-30 | 1996-08-06 | Elf Atochem North America, Inc. | Paint strippers process |
US5817612A (en) * | 1991-01-30 | 1998-10-06 | Elf Atochem North America, Inc. | Aqueous benzyl formate paint stripper |
WO1992014785A1 (en) * | 1991-02-15 | 1992-09-03 | Kuraray Co., Ltd. | Aqueous dispersion and base material coated therewith |
US5272200A (en) * | 1991-02-15 | 1993-12-21 | Kuraray Co., Ltd. | Aqueous dispersion and substrate coated with the same |
US5726140A (en) * | 1992-06-02 | 1998-03-10 | Elf Atochem North America, Inc. | Water-in-oil emulsion having aqueous phase evaporation retarded with wax |
US5780409A (en) * | 1992-06-02 | 1998-07-14 | Elf Atochem North America, Inc. | Water-in-oil emulsion having aqueous phase evaporation retarded with wax IR 3323D |
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