JPH0661915B2 - Laminate - Google Patents
LaminateInfo
- Publication number
- JPH0661915B2 JPH0661915B2 JP4767491A JP4767491A JPH0661915B2 JP H0661915 B2 JPH0661915 B2 JP H0661915B2 JP 4767491 A JP4767491 A JP 4767491A JP 4767491 A JP4767491 A JP 4767491A JP H0661915 B2 JPH0661915 B2 JP H0661915B2
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Description
【0001】[0001]
【産業上の利用分野】本発明は、塩化ビニル系樹脂及び
塩化ビニリデン系樹脂との接着性に著るしく秀れたグラ
フト変性樹脂組成物を用いた当該樹脂との積層体に関す
るものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a laminate of a vinyl chloride resin and a vinylidene chloride resin, using a graft-modified resin composition having excellent adhesiveness to the resin.
【0002】[0002]
【従来の技術】塩化ビニル系樹脂又は塩化ビニリデン系
樹脂は、ガスバリヤー性に秀れ、かつ耐油性、耐薬品性
等にも良好な事より、種々の包装材料、特に食品包装材
料として好適である。2. Description of the Related Art Vinyl chloride resins or vinylidene chloride resins are suitable as various packaging materials, especially food packaging materials, because they have excellent gas barrier properties, oil resistance and chemical resistance. is there.
【0003】しかしながらこれらの樹脂は、概して通常
のヒートシール性に乏しい為、該ヒートシール性の良好
な樹脂例えば、ポリオレフィン系樹脂と積層して使用さ
れる事が多く、この積層体は両者の特長を兼ね備えた秀
れた包装材料となる。ところがこれらの樹脂は、ポリオ
レフィン系樹脂とは本質的に接着が困難で、両者の素材
間には、接着剤の介在が不可欠となる。However, since these resins are generally poor in ordinary heat-sealing property, they are often used by laminating with a resin having a good heat-sealing property, for example, a polyolefin resin, and this laminated body has the advantages of both. It becomes an excellent packaging material that combines both. However, it is essentially difficult to bond these resins to the polyolefin resin, and it is necessary to interpose an adhesive between the two materials.
【0004】かかる接着剤としては、既に種々の酸グラ
フト変性ポリオレフィンが提案され実際ポリアミド系樹
脂やエチレンビニルアルコール共重合体との積層体に接
着層として使用されているが、特に塩化ビニル系樹脂及
び塩化ビニリデン系樹脂との接着性に於いては未だ不充
分であり、更に強固な接着性を有する樹脂の出現が強く
市場で要望されている。As such an adhesive, various acid-grafted modified polyolefins have already been proposed and actually used as an adhesive layer in a laminate with a polyamide resin or an ethylene vinyl alcohol copolymer. In particular, vinyl chloride resins and Adhesiveness with vinylidene chloride resin is still insufficient, and the appearance of a resin having stronger adhesiveness is strongly demanded in the market.
【0005】塩化ビニル系樹脂又は塩化ビニリデン系樹
脂を包装材料として使用する場合、フィルムとして必要
な柔軟性等の性質を付与する為これらの樹脂に適当な可
塑剤を必要量加えるが、この可塑剤を含むいわゆる軟質
性の塩化ビニル系樹脂とポリオレフィン系樹脂の熱接着
はとりわけ難かしく、この傾向は可塑剤量が多い程即
ち、軟質になればなる程大きい。これは、塩化ビニル系
樹脂の表面にこの可塑剤がブリードしてポリオレフィン
との接着がこの可塑剤によって阻害される為であると考
えられる。当然、層間の接着性が不充分であると、耐油
性、耐熱性に悪影響を及ぼすばかりでなく、ヒートシー
ル強度にも大きく影響を及ぼし結果としてヒートシール
不充分となり実用に供しなくなる。When a vinyl chloride resin or vinylidene chloride resin is used as a packaging material, a suitable amount of a plasticizer is added to these resins in order to impart properties such as flexibility required as a film. It is particularly difficult to thermally bond a so-called soft vinyl chloride resin containing a polyolefin resin with a polyolefin resin, and this tendency becomes greater as the amount of the plasticizer increases, that is, the softer it becomes. It is considered that this is because the plasticizer bleeds on the surface of the vinyl chloride resin and the adhesion with the polyolefin is hindered by the plasticizer. As a matter of course, if the adhesion between the layers is insufficient, not only the oil resistance and heat resistance are adversely affected, but also the heat sealing strength is greatly affected, resulting in insufficient heat sealing, which makes it unusable for practical use.
【0006】[0006]
【発明が解決しようとする課題】従って本発明はこれら
接着性の悪い樹脂との接着性のよい材料を見出し、これ
を用いて塩化ビニル樹脂等との積層体を提供することを
目的とする。SUMMARY OF THE INVENTION It is therefore an object of the present invention to find a material having good adhesiveness with these resins having poor adhesiveness, and using this material to provide a laminate with a vinyl chloride resin or the like.
【0007】[0007]
【課題を解決するための手段】そこで本発明者は、この
可塑剤による接着阻害を超えて塩化ビニル系樹脂又は、
塩化ビニリデン系樹脂と強固に熱接着する接着性樹脂組
成物及びこれを用いたバリヤー性耐油性、シール性に秀
れた積層体について鋭意検討した結果、本発明に到達し
たものである。本発明の要旨は、酢酸ビニル含量3〜5
0wt%のエチレン−酢酸ビニル共重合体1〜99重量部
と、アクリル酸エステル含量もしくはメタクリル酸エス
テル含量0.1〜30wt%且つ無水マレイン酸含量0.
05〜20wt%のエチレン−アクリル酸エステル−無水
マレイン酸三元共重合体又はエチレン−メタクリル酸エ
ステル−無水マレイン酸三元共重合体99〜1重量部か
らなる樹脂組成物100重量部に対し、ラジカル発生剤
0.001〜0.5重量部の存在下に不飽和カルボン酸
又はその無水物を前記共重合体又は三元共重合体にグラ
フト変性してなる接着性樹脂組成物層と、塩化ビニル系
樹脂層又は塩化ビニリデン系樹脂層とからなる積層体に
ある。Therefore, the present inventor has found that the vinyl chloride resin or
The present invention has been achieved as a result of extensive studies on an adhesive resin composition that strongly thermally adheres to a vinylidene chloride resin and a laminate using the same and having excellent barrier properties, oil resistance, and sealing properties. The gist of the present invention is that the vinyl acetate content is 3 to 5
1 to 99 parts by weight of an ethylene-vinyl acetate copolymer of 0 wt%, an acrylic acid ester content or a methacrylic acid ester content of 0.1 to 30 wt% and a maleic anhydride content of 0.
With respect to 100 parts by weight of a resin composition consisting of 99 to 1 part by weight of an ethylene-acrylic acid ester-maleic anhydride terpolymer or ethylene-methacrylic acid ester-maleic anhydride terpolymer of 05 to 20 wt%, An adhesive resin composition layer obtained by graft-modifying an unsaturated carboxylic acid or an anhydride thereof to the above-mentioned copolymer or terpolymer in the presence of 0.001 to 0.5 part by weight of a radical generator; And a vinyl resin layer or a vinylidene chloride resin layer.
【0008】以下、本発明について詳細に詳述する。本
発明において、グラフト変性に用いる一方の樹脂として
のエチレン−酢酸ビニル共重合体(以下EVAと略す
る)は、酢酸ビニル含量(以下、酢ビ含量と略する)が
3〜50wt%好ましくは10〜35wt%であり、メルト
フローレート(JIS K6760による、以下同様)
としては0.5〜300g/10min 好ましくは1〜3
0g/10min であり、樹脂組成物において1〜99重
量部好ましくは30〜90重量部を用いる。このEVA
においては酢ビ含量が3wt%未満の場合、接着性が不充
分であり、50wt%を越えると押出成形性が低下し、又
メルトフローレートが0.5g/10min 未満だったり
300g/10min を越えても押出成形性が低下する。The present invention will be described in detail below. In the present invention, the ethylene-vinyl acetate copolymer (hereinafter abbreviated as EVA) as one resin used for graft modification has a vinyl acetate content (hereinafter abbreviated as vinyl acetate content) of 3 to 50 wt%, preferably 10 ~ 35 wt%, melt flow rate (according to JIS K6760, the same applies hereinafter)
As 0.5-300 g / 10 min, preferably 1-3
It is 0 g / 10 min, and 1 to 99 parts by weight, preferably 30 to 90 parts by weight, is used in the resin composition. This EVA
When the vinyl acetate content is less than 3 wt%, the adhesiveness is insufficient, and when it exceeds 50 wt%, the extrusion moldability decreases, and the melt flow rate is less than 0.5 g / 10 min or more than 300 g / 10 min. However, the extrusion moldability is reduced.
【0009】又、グラフト変性に用いる他方の樹脂とし
てのエチレン−アクリル酸エステル−無水マレイン酸三
元共重合体又はエチレン−メタクリル酸エステル−無水
マレイン酸三元共重合体は、アクリル酸エステル含量又
はメタクリル酸エステル含量0.1〜30wt%好ましく
は5〜20wt%、無水マレイン酸含量0.05〜20wt
%好ましくは0.1〜10wt%を含むエチレンとの三元
共重合体であり、メルトフローレートとしては特に規定
するものではないが0.5〜150g/10min 好まし
くは1〜50g/10min であり、樹脂組成物において
99〜1重量部好ましくは30〜10重量部を用いる。
この三元共重合体においては前記エステル含量が5wt%
未満、前記無水マレイン酸含量が0.05wt%未満では
接着性が不充分であり、前記エステル含量が30wt%を
越えると接着性が低下し、前記無水マレイン酸含量が2
0wt%を越えると押出成形性が低下し、又メルトフロー
レートが0.5g/10min 未満だったり150g/1
0min を越えても押出成形性が低下する。The ethylene-acrylic acid ester-maleic anhydride terpolymer or the ethylene-methacrylic acid ester-maleic anhydride terpolymer as the other resin used for graft modification has an acrylic acid ester content or Methacrylic acid ester content 0.1 to 30 wt%, preferably 5 to 20 wt%, maleic anhydride content 0.05 to 20 wt%
%, Preferably a terpolymer with 0.1 to 10 wt% of ethylene, and the melt flow rate is not particularly specified, but 0.5 to 150 g / 10 min, preferably 1 to 50 g / 10 min. The resin composition is used in an amount of 99 to 1 part by weight, preferably 30 to 10 parts by weight.
In this terpolymer, the ester content is 5 wt%
If the maleic anhydride content is less than 0.05 wt%, the adhesiveness is insufficient, and if the ester content exceeds 30 wt%, the adhesiveness decreases, and the maleic anhydride content is 2% or less.
If it exceeds 0 wt%, the extrusion moldability will deteriorate, and the melt flow rate will be less than 0.5 g / 10 min or 150 g / 1.
Even if it exceeds 0 min, the extrusion moldability deteriorates.
【0010】アクリル酸エステルとしては、アクリル酸
メチル、アクリル酸エチル、アクリル酸ブチル、アクリ
ル酸2−エチルヘキシル等が、メタクリル酸エステルと
しては、メタクリル酸メチル、メタクリル酸エチル、メ
タクリル酸ブチル等が挙げられ、特にアクリル酸メチ
ル、アクリル酸エチル、メタクリル酸メチルが好まし
い。Examples of the acrylate ester include methyl acrylate, ethyl acrylate, butyl acrylate, 2-ethylhexyl acrylate, and the like, and examples of the methacrylate ester include methyl methacrylate, ethyl methacrylate, butyl methacrylate, and the like. Especially, methyl acrylate, ethyl acrylate, and methyl methacrylate are preferable.
【0011】この樹脂組成物は配合比においてEVAが
99重量部を越えると特に塩化ビニル系樹脂又は塩化ビ
ニリデン系樹脂との接着性が低下し、前記三元共重合体
が99重量部を越えても接着性が不足する。この樹脂組
成物100重量部に対しラジカル発生剤0.001〜
0.5重量部好ましくは0.05〜0.3重量部の存在
下、不飽和カルボン酸又はその無水物を添加し、前記樹
脂組成物をグラフト変性せしめる。ラジカル発生剤が
0.001重量部未満では接着性が不十分となり、0.
5重量部を越えると架橋によるゲルが発生し商品価値を
低下せしめるばかりでなく、接着性や押出成形性にも悪
影響を与える。When the EVA exceeds 99 parts by weight in the compounding ratio, the adhesiveness with a vinyl chloride resin or vinylidene chloride resin deteriorates, and the terpolymer exceeds 99 parts by weight. Also lacks adhesiveness. Radical generator 0.001 to 100 parts by weight of this resin composition
In the presence of 0.5 part by weight, preferably 0.05 to 0.3 part by weight, unsaturated carboxylic acid or its anhydride is added to graft-modify the resin composition. If the amount of the radical generator is less than 0.001 part by weight, the adhesiveness will be insufficient, and
If the amount exceeds 5 parts by weight, gel due to cross-linking is generated and not only the commercial value is lowered but also the adhesiveness and the extrusion moldability are adversely affected.
【0012】グラフト変性に用いるラジカル発生剤とし
ては、ジクミルパーオキサイド、ベンゾイルパーオキサ
イド、ジ−t−ブチルパーオキサイド、2,5−ジメチ
ル−2,5−ジ(t−ブチルパーオキシ)ヘキサン、
2,5−ジメチル−2,5−ジ(t−ブチルパーオキ
シ)ヘキセン−3、ラウロイルパーオキサイド、t−ブ
チルパーオキシベンゾエート等の有機過酸化物が好まし
く使用され、2種以上組合せでも良い。Radical generators used for graft modification include dicumyl peroxide, benzoyl peroxide, di-t-butyl peroxide, 2,5-dimethyl-2,5-di (t-butylperoxy) hexane,
Organic peroxides such as 2,5-dimethyl-2,5-di (t-butylperoxy) hexene-3, lauroyl peroxide and t-butylperoxybenzoate are preferably used, and a combination of two or more kinds may be used.
【0013】グラフト変性に用いるモノマーである不飽
和カルボン酸又はその無水物としては、アクリル酸、マ
レイン酸、フマール酸、イタコン酸、ハイミック酸又は
それらの無水物が挙げられ、中でもアクリル酸、マレイ
ン酸、無水マレイン酸又は無水ハイミック酸が好まし
い。勿論これらは、2種以上組み合せて使用しても良
い。グラフト変性は、適当な溶媒中に懸濁又は溶解して
いる前述の樹脂組成物にグラフト変性用モノマー及びラ
ジカル発生剤を添加して加熱攪拌する方法、該樹脂組成
物と上記モノマー及びラジカル発生剤を予め混合し押出
機、バンバリーミキサー、ニーダー等を用いて溶融混練
する方法等があるが、マレイン酸、無水マレイン酸、無
水ハイミック酸等を用いてグラフト変性する場合は、後
者の方法が好んで採用される。なおグラフト変性量は特
に制限するものではないが樹脂組成物100重量部に対
し0.0001〜3重量部でよい。Examples of the unsaturated carboxylic acid or its anhydride used as a monomer for the graft modification include acrylic acid, maleic acid, fumaric acid, itaconic acid, hymic acid and their anhydrides, among which acrylic acid and maleic acid. , Maleic anhydride or hymic acid anhydride are preferred. Of course, these may be used in combination of two or more kinds. The graft modification is carried out by adding a monomer for graft modification and a radical generator to the above resin composition suspended or dissolved in a suitable solvent and stirring the mixture, the resin composition and the monomer and radical generator. There are methods such as pre-mixing and melt-kneading using an extruder, Banbury mixer, kneader, etc., but in the case of graft modification with maleic acid, maleic anhydride, hymic acid anhydride, etc., the latter method is preferred. Adopted. The amount of graft modification is not particularly limited, but may be 0.0001 to 3 parts by weight with respect to 100 parts by weight of the resin composition.
【0014】本発明のこうして得られたグラフト変性さ
れた接着性樹脂組成物は、塩化ビニル系樹脂層又は塩化
ビニリデン系樹脂層を接合する積層体において特に秀れ
た接着性を示すが、接合の方法としては、例えば共押出
成形、押出コーティング、ドライラミネート、各種熱溶
着法等いずれの方法も採用する事ができ、さらにポリオ
レフィン系樹脂層をはじめ異樹脂層を重ねた所望の積層
体も得られるが、特に各樹脂を別々の押出機により溶融
押出して円形ダイ、T−ダイ等の内部又は押出し直後で
各層を接合させて所望の形状の多層フィルム、多層シー
ト、多層ブローボトル等を得る方法即ち共押出成形が経
済的な面で有利である。成形温度は、各樹脂の軟化温度
以上、分解温度以下であれば成形が可能である。共押出
成形の場合は、各層を構成する樹脂の溶融粘度が極端に
異なっていない方が、接着性、成形性及び物性の面で望
ましい。The thus obtained graft-modified adhesive resin composition of the present invention exhibits particularly excellent adhesiveness in a laminate for joining a vinyl chloride resin layer or a vinylidene chloride resin layer. As a method, for example, any method such as coextrusion molding, extrusion coating, dry laminating, various heat welding methods, etc. can be adopted, and a desired laminate having different resin layers including a polyolefin resin layer can be obtained. However, in particular, a method for obtaining a multilayer film, a multilayer sheet, a multilayer blow bottle, etc. having a desired shape by melt-extruding each resin by a separate extruder and joining each layer inside a circular die, a T-die or immediately after extrusion, that is, Coextrusion is economically advantageous. Molding is possible if the molding temperature is higher than the softening temperature of each resin and lower than the decomposition temperature. In the case of coextrusion molding, it is desirable that the melt viscosities of the resins forming the layers are not extremely different from the viewpoint of adhesiveness, moldability and physical properties.
【0015】[0015]
【実施例】以下に実施例、比較例を挙げて本発明を更に
詳細に説明する。 実施例1〜6、比較例1〜2 メルトフローレート6.0g/10min 、酢ビ含量19
wt%のエチレン−酢酸ビニル共重合体(以下、EVAと
略する)とメルトフローレート3.2g/10min 、ア
クリル酸メチル(以下、MAと略する)含量3wt%、無
水マレイン酸(以下、MAHと略する)含量0.4wt%
のエチレン−MA−MAH三元共重合体(以下、EMA
Hと略する)を表1の割でヘンシェルミキサーで混合
し、これにジ−t−ブチルパーオキサイドを上記樹脂混
合物100重量部に対し、0.012重量部添加し、ペ
レット表面を均一にぬらした後、無水マレイン酸を0.
7重量部添加してヘンシェルミキサーで均一な混合物と
し、これを40mmφ押出機を用いて200℃で溶融混合
押出してグラフト変性接着性樹脂組成物を得た。共押出
フィルム成形装置を用い、このグラフト変性接着性樹脂
組成物をシリンダー温度180℃、ダイ温度180℃
で、30重量%のDOP(ジオクチルフタレート)を含
むポリ塩化ビニル樹脂(以下、PVCと略する)をシリ
ンダー温度170℃、ダイ温度180℃で2種2層の共
押出フィルム(接着性樹脂層組成物20μ厚、PVC層
60μ厚)を得た。この共押出フィルムを幅15mm、長
さ15cmに切り、その一端を強制剥離して、テンシロン
型引張試験機を用い、引張速度100mm/min 、180
度剥離の条件で剥離強度を測定した。その結果も表1に
示すが剥離強度は実施例1〜6において秀れ、EVA又
はEMAHの多すぎる比較例1〜2において弱かった。EXAMPLES The present invention will be described in more detail below with reference to examples and comparative examples. Examples 1-6, Comparative Examples 1-2 Melt flow rate 6.0 g / 10 min, vinyl acetate content 19
wt% ethylene-vinyl acetate copolymer (hereinafter abbreviated as EVA), melt flow rate 3.2 g / 10 min, methyl acrylate (hereinafter abbreviated as MA) content 3 wt%, maleic anhydride (hereinafter MAH) Abbreviated) content 0.4 wt%
Ethylene-MA-MAH terpolymer (hereinafter referred to as EMA
(Abbreviated as H) is mixed by a Henschel mixer in the ratio shown in Table 1, and 0.012 parts by weight of di-t-butyl peroxide is added to 100 parts by weight of the above resin mixture to evenly wet the pellet surface. And then maleic anhydride was reduced to 0.
7 parts by weight was added to make a uniform mixture with a Henschel mixer, and this was melt-mixed and extruded at 200 ° C. using a 40 mmφ extruder to obtain a graft-modified adhesive resin composition. Using a coextrusion film molding machine, the graft modified adhesive resin composition was subjected to a cylinder temperature of 180 ° C. and a die temperature of 180 ° C.
Then, a polyvinyl chloride resin (hereinafter abbreviated as PVC) containing 30% by weight of DOP (dioctyl phthalate) is used as a coextrusion film of two kinds and two layers (adhesive resin layer composition) at a cylinder temperature of 170 ° C. and a die temperature of 180 ° C. 20 μm thick, PVC layer 60 μm thick) were obtained. This co-extruded film is cut into a piece having a width of 15 mm and a length of 15 cm, and one end thereof is forcibly peeled off. A tensile speed of 100 mm / min, 180
The peel strength was measured under the condition of peeling once. The results are also shown in Table 1, but the peel strength was excellent in Examples 1 to 6 and weak in Comparative Examples 1 and 2 containing too much EVA or EMAH.
【0016】[0016]
【表1】 [Table 1]
【0017】実施例7〜11、比較例3〜4 メルトフローレート15g/10min 、酢ビ含量25wt
%のEVAと、メルトフローレート3.8g/10min
、メタクリル酸エチル(以下、EMAと略する)含量
4.5wt%、MAH1.3wt%のエチレン−EMA−M
AH三元共重合体(以下、EEMAHと略する)と表2
に示す割合で行なった他は実施例1〜6と同様にしてグ
ラフト変性樹脂組成物を得、同様の方法で剥離強度を測
定した。その結果を表2に示すが剥離強度は実施例7〜
11において秀れ、EVA又はEEMAHの多すぎる比
較例3,4において弱かった。Examples 7-11, Comparative Examples 3-4 Melt flow rate 15 g / 10 min, vinyl acetate content 25 wt.
% EVA and melt flow rate 3.8 g / 10 min
Ethylene-EMA-M with an ethyl methacrylate (hereinafter abbreviated as EMA) content of 4.5 wt% and MAH of 1.3 wt%
AH terpolymer (hereinafter abbreviated as EEMAH) and Table 2
A graft-modified resin composition was obtained in the same manner as in Examples 1 to 6 except that the ratio shown in Table 1 was used, and the peel strength was measured by the same method. The results are shown in Table 2, and the peel strengths of Examples 7 to
11 was excellent, and it was weak in Comparative Examples 3 and 4 having too much EVA or EEMAH.
【0018】[0018]
【表2】 [Table 2]
【0019】実施例12〜15 メルトフローレート7g/10min 、メタクリル酸メチ
ル(以下、MMAと略する)含量8wt%、MAH2.9
wt%のエチレン−MMA−MAH三元共重合体(以下、
EMMAHと略する)を表3に示す割合で行なった他は
実施例1〜6と同様にしてグラフト変性樹脂を得、同様
の方法で剥離強度を測定した。その結果を表3に示す
が、いずれもPVCとの接着性は秀れていた。Examples 12 to 15 Melt flow rate 7 g / 10 min, methyl methacrylate (hereinafter abbreviated as MMA) content 8 wt%, MAH 2.9
wt% ethylene-MMA-MAH terpolymer (hereinafter,
A graft-modified resin was obtained in the same manner as in Examples 1 to 6 except that EMMAH was abbreviated as shown in Table 3, and the peel strength was measured by the same method. The results are shown in Table 3, and all of them showed excellent adhesion to PVC.
【0020】[0020]
【表3】 [Table 3]
Claims (1)
−酢酸ビニル共重合体1〜99重量部と、アクリル酸エ
ステル含量もしくはメタクリル酸エステル含量0.1〜
30wt%且つ無水マレイン酸含量0.05〜20wt%の
エチレン−アクリル酸エステル−無水マレイン酸三元共
重合体又はエチレン−メタクリル酸エステル−無水マレ
イン酸三元共重合体99〜1重量部からなる樹脂組成物
100重量部に対し、ラジカル発生剤0.001〜0.
5重量部の存在下に不飽和カルボン酸又はその無水物を
前記共重合体又は三元共重合体にグラフト変性してなる
接着性樹脂組成物層と、塩化ビニル系樹脂層又は塩化ビ
ニリデン系樹脂層とからなる積層体。1. An ethylene-vinyl acetate copolymer having a vinyl acetate content of 3 to 50 wt%, 1 to 99 parts by weight, an acrylic acid ester content or a methacrylic acid ester content of 0.1 to 10.
It comprises 99-1 parts by weight of ethylene-acrylic acid ester-maleic anhydride terpolymer or ethylene-methacrylic acid ester-maleic anhydride terpolymer of 30 wt% and maleic anhydride content of 0.05-20 wt%. With respect to 100 parts by weight of the resin composition, the radical generator 0.001 to 0.
An adhesive resin composition layer obtained by graft-modifying an unsaturated carboxylic acid or its anhydride in the presence of 5 parts by weight to the above-mentioned copolymer or terpolymer, a vinyl chloride resin layer or a vinylidene chloride resin A laminate consisting of layers.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4767491A JPH0661915B2 (en) | 1991-02-20 | 1991-02-20 | Laminate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4767491A JPH0661915B2 (en) | 1991-02-20 | 1991-02-20 | Laminate |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18683482A Division JPS5975914A (en) | 1982-10-26 | 1982-10-26 | Adhesive resin and its laminate |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04261846A JPH04261846A (en) | 1992-09-17 |
JPH0661915B2 true JPH0661915B2 (en) | 1994-08-17 |
Family
ID=12781821
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4767491A Expired - Lifetime JPH0661915B2 (en) | 1991-02-20 | 1991-02-20 | Laminate |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0661915B2 (en) |
-
1991
- 1991-02-20 JP JP4767491A patent/JPH0661915B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH04261846A (en) | 1992-09-17 |
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