JPH0611832B2 - Resin composition of saponified ethylene copolymer - Google Patents

Resin composition of saponified ethylene copolymer

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Publication number
JPH0611832B2
JPH0611832B2 JP15229985A JP15229985A JPH0611832B2 JP H0611832 B2 JPH0611832 B2 JP H0611832B2 JP 15229985 A JP15229985 A JP 15229985A JP 15229985 A JP15229985 A JP 15229985A JP H0611832 B2 JPH0611832 B2 JP H0611832B2
Authority
JP
Japan
Prior art keywords
resin composition
copolymer
polyamide
parts
film
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 - Lifetime
Application number
JP15229985A
Other languages
Japanese (ja)
Other versions
JPS6213449A (en
Inventor
博造 上條
研司 清水
一信 佐野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ube Corp
Original Assignee
Ube Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ube Industries Ltd filed Critical Ube Industries Ltd
Priority to JP15229985A priority Critical patent/JPH0611832B2/en
Priority to US06/883,078 priority patent/US4749744A/en
Priority to DE8686305302T priority patent/DE3683974D1/en
Priority to EP86305302A priority patent/EP0214724B1/en
Publication of JPS6213449A publication Critical patent/JPS6213449A/en
Publication of JPH0611832B2 publication Critical patent/JPH0611832B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は,エチレン系共重合体ケン化物の樹脂組成物
に関するものである。詳しくは,エチレン−酢酸ビニル
共重合体が高度にケン化されているケ化物に,特定のポ
リアミドが特定の割合で配合されている樹脂組成物に係
るものである。この発明の樹脂組成物から押出成形によ
り成形されたフィルムまたは容器は,ガスバリヤー性お
よび耐衝撃性(耐ピンホール性)が共に優れており,特
に食品の包装用フィルムまたは容器に好適に使用するこ
とができる。また,本発明の樹脂組成物から射出成形に
より成形された成形品は,剛性・耐熱性だけでなく衝撃
強度も優れており,エンジニアリングプラスチックスと
して各種機能部品に使用することができる。
The present invention relates to a resin composition of a saponified ethylene-based copolymer. More specifically, the present invention relates to a resin composition in which a specific polyamide is blended in a specific ratio with a highly saponified ethylene-vinyl acetate copolymer. A film or container formed by extrusion molding from the resin composition of the present invention has both excellent gas barrier properties and impact resistance (pinhole resistance), and is particularly suitable for use as a film or container for packaging foods. be able to. Further, the molded product formed by injection molding from the resin composition of the present invention has excellent impact strength as well as rigidity and heat resistance, and can be used as engineering plastics for various functional parts.

〔従来技術の説明〕[Description of Prior Art]

一般に,エチレン−酢酸ビニル共重合体のケン化物(以
下,EVOHと略記する。)は,ガスバリヤー性が極め
て良好なために,酸素ガス透過速度の小さいことが要求
される食品包装用フィルムまたは容器を形成する材料と
して使用される。また,EVOHに特にガラス繊維を配
合したものは剛性・耐熱性が高いため,金属部品(Al
ダイカスト,Znダイカスト等)の代替として各種機能
部品に使用される。
In general, a saponified product of an ethylene-vinyl acetate copolymer (hereinafter abbreviated as EVOH) has a very good gas barrier property, and therefore, a film or container for food packaging which is required to have a low oxygen gas permeation rate. Used as a material for forming In addition, EVOH with glass fiber in particular has high rigidity and heat resistance, so metal parts (Al
It is used for various functional parts as an alternative to die casting, Zn die casting, etc.).

しかし,このEVOHはその成形物が硬くて脆いという
欠点を有しており用途面で制約を受けている。例えば,
食品包装用のフィルム・シートとして使用する場合に,
包装作業時,包装品の移動作業時,輸送作業時に,その
フィルムが破れたり,ピンホールを生じたりし易く,そ
の優れたガスバリヤー性を十分に生かすことができない
でいる。さらに,射出成形品で使用する場合でも,特に
成形直後及び低温時にクラック発生等のクレームが起る
ことが多かった。
However, this EVOH has the drawback that its molded product is hard and brittle, and is limited in its application. For example,
When used as a film or sheet for food packaging,
During the packaging work, the movement work of the packaged goods, and the transportation work, the film is easily broken or pinholes are easily generated, and the excellent gas barrier property cannot be fully utilized. Furthermore, even when used in injection-molded products, there were many complaints about cracks, especially immediately after molding and at low temperatures.

一般にEVOHの物性及び成形性はエチレン含量および
ケン化度により変化し,エチレン含量が増すにつれ,ま
たケン化度が小さくなるにつれて,成形性や耐衝撃性は
良好となるが,逆にガスバリヤー性,剛性,耐熱性は低
下していく。このため,EVOHの特徴であるガスバリ
ヤー性,剛性,耐熱性を大きく損わず,耐衝撃性を改良
する新しい技術が強く期待されていた。
Generally, the physical properties and moldability of EVOH change depending on the ethylene content and saponification degree. As the ethylene content increases and as the saponification degree decreases, the moldability and impact resistance become better, but conversely the gas barrier property. , Rigidity and heat resistance will decrease. Therefore, a new technique for improving impact resistance without greatly impairing the gas barrier property, rigidity, and heat resistance, which are the characteristics of EVOH, has been strongly expected.

このようなEVOHの欠点を改良する手段としては,E
VOHに各種のポリアミドを混合した樹脂組成物を使用
する方法が,例えば,特公昭44−24277号公報,
48−22833号公報,特開昭50−121347号
公報,特開昭54−78749号公報,特開昭54−7
8750号公報,特開昭55−34956号公報などに
よって,よく知られている。
As a means for improving such a drawback of EVOH, E
A method of using a resin composition in which various polyamides are mixed with VOH is disclosed in, for example, Japanese Patent Publication No. 44-24277.
48-22833, JP-A-50-121347, JP-A-54-78749, JP-A-54-7.
It is well known from Japanese Patent No. 8750 and Japanese Patent Laid-Open No. 55-34956.

前記の方法は,EVOHとポリアミドが互いに相溶性の
よいものであるため,EVOHにポリアミドを配合して
混合すれば,ポリアミドガ耐衝撃性を改善するように作
用し,しかもEVOHの本来の優れたガスバリヤー性,
剛性,耐熱性をあまり損なわないのである。
In the above method, EVOH and polyamide have good compatibility with each other. Therefore, if polyamide is blended with EVOH and blended, it acts to improve the impact resistance of polyamide polyamide, and furthermore, EVOH has excellent original properties. Gas barrier property,
The rigidity and heat resistance are not significantly impaired.

しかし,このEVOHとポリアミドとの混合物である樹
脂組成物では,大きな問題点がある。
However, this resin composition, which is a mixture of EVOH and polyamide, has a serious problem.

すなわち,EVOHとポリアミドとを溶融状態で混合す
ると,両者が化学反応を起こして溶融粘度が増加し,最
終的にはゲル化してしまい,成形ができなくなってしま
う。
That is, when EVOH and polyamide are mixed in a molten state, a chemical reaction occurs between the two, the melt viscosity increases, and finally gelation occurs, making molding impossible.

このゲル化は,成形温度が高い程顕著となるため,ポリ
アミドとしては融点の低い各種の共重合ポリアミドを使
用する手段が提案されており,それらの方法としては,
例えば,特開昭54−78749号公報,特開昭54−
78750号公報,特開昭55−34956号公報など
に開示されている方法を挙げることができる。
Since this gelation becomes more remarkable as the molding temperature becomes higher, means for using various copolyamides having a low melting point as polyamides have been proposed.
For example, JP-A-54-78749 and JP-A-54-
The methods disclosed in JP-A-78750 and JP-A-55-34956 can be mentioned.

しかし,これらの方法でもゲル化を完全に防止すること
は困難であり,成形加工性を損なうことなく,EVOH
の耐衝撃性を改良する実用的な方法が望まれている。
However, even with these methods, it is difficult to completely prevent gelation, and EVOH can be used without impairing moldability.
There is a demand for a practical method for improving the impact resistance of the.

〔本発明の各要件および作用効果〕[Each requirement and effect of the present invention]

本発明者らは,このようなEVOHの耐衝撃性を改良す
べく鋭意研究した結果,特定のEVOHに特定の末端基
変性を行ったポリアミドを混合した樹脂組成物は,その
成形時にゲル化が起こりにくく,しかも成形物のガスバ
リヤー性,剛性,耐熱性を損なうことがなく,さらに耐
ピンホール性あるいは耐衝撃性が改良されることを見い
だし,この発明を完成した。
As a result of intensive studies aimed at improving the impact resistance of such EVOH, the present inventors have found that a resin composition obtained by mixing a specific EVOH with a polyamide modified with a specific end group shows no gelation during molding. The inventors have found that it is unlikely to occur, do not impair the gas barrier properties, rigidity, and heat resistance of the molded product, and further improve pinhole resistance or impact resistance, and completed the present invention.

すなわち,この発明はエチレンモノマーに基づく反復単
位(−CH2−CH2)を5〜50モル%有していると共に,
ケン化度が80%以上であるエチレンと酢酸ビニルとの
共重合体のケン化物100重量部と,相対粘度が2.1
〜3.5で,かつ,アミノ末端基が8×10-5当量/g
以上で,カルボキシ末端基が3×10-5当量/g以下で
あるアミノ末端リッチの末端変性されたポリアミド5〜
150重量部とからなることを特徴とするエチレン系共
重合体ケン化物の樹脂組成物に関するものである。
That is, the present invention has 5 to 50 mol% of repeating units (—CH 2 —CH 2 ) based on ethylene monomer, and
100 parts by weight of a saponified product of a copolymer of ethylene and vinyl acetate having a saponification degree of 80% or more, and a relative viscosity of 2.1.
~ 3.5 and the amino end group is 8 × 10 -5 equivalent / g
Thus, the amino-terminal rich end-modified polyamide having a carboxyl end group of 3 × 10 −5 equivalent / g or less 5 to 5
It relates to a resin composition of a saponified ethylene-based copolymer, which is characterized by comprising 150 parts by weight.

この発明の樹脂組成物は, (a) フィルム,容器,射出成形品などの成形の際に,
ゲル化したりして,成形が困難となることがなく,しか
も, (b) その成形物が,十分なガスバリヤー性,剛性,耐
熱性を有すると共に,耐ピンボール性あるいは耐衝撃性
が改良されているので,包装材料あるいは機能性部品と
して好適に使用することができる。
The resin composition of the present invention (a) is used for molding films, containers, injection molded products,
Molding does not become difficult due to gelation, and (b) the molded product has sufficient gas barrier properties, rigidity, heat resistance, and improved pinball resistance or impact resistance. Therefore, it can be suitably used as a packaging material or a functional component.

〔本発明の各要件の詳しい説明〕[Detailed description of each requirement of the present invention]

本発明に使用するエチレンと酢酸ビニルとの共重合体の
ケン化物(EVOH)は,エチレンモノマーに基づく反
復単位Iを,ポリマーの全量に対して5〜50モル%,
好ましくは10〜45モル%,特に好ましくは15〜4
0モル%の割合で有していると共に,ケン化度が80%
以上,好ましくは90%以上,特に好ましくは95%以
上である『エチレン−酢酸ビニル共重合体ケン化物』で
ある。
The saponified product (EVOH) of a copolymer of ethylene and vinyl acetate used in the present invention contains repeating units I based on ethylene monomer in an amount of 5 to 50 mol% based on the total amount of the polymer.
Preferably 10 to 45 mol%, particularly preferably 15 to 4
It has a proportion of 0 mol% and a saponification degree of 80%.
As described above, the "saponified ethylene-vinyl acetate copolymer" is preferably 90% or more, and particularly preferably 95% or more.

前記のケン化物(EVOH)は,エチレンモノマーと酢
酸ビニルモノマーを公知の方法で重合して得られたエチ
レン−酢酸ビニル共重合体をケン化して製造されるもの
であり,エチレンモノマーに基づく前記反復単位Iがケ
ン化物に対して5モル%より少ないと,そのようなケン
化物を使用して得られた樹脂組成物の成形性が悪くなる
ので適当でなく,一方,エチレンモノマーに基づく前記
反復単位Iを50モル%より多く有する場合には,その
ようなケン化物を配合した樹脂組成物から成形される成
形物のガスバリヤー性,剛性,耐熱性が悪化するので適
当でない。
The saponified product (EVOH) is prepared by saponifying an ethylene-vinyl acetate copolymer obtained by polymerizing an ethylene monomer and a vinyl acetate monomer by a known method, and the repeating product based on the ethylene monomer is used. If the unit I is less than 5 mol% with respect to the saponified product, the moldability of the resin composition obtained using such a saponified product is deteriorated, which is not suitable. On the other hand, the repeating unit based on the ethylene monomer is not suitable. When the content of I is more than 50 mol%, the gas barrier property, rigidity and heat resistance of the molded product molded from the resin composition containing such a saponified product are deteriorated, which is not suitable.

この発明では,EVOHの重合度などは,特別に制限さ
れないが,極限粘度(15重量%含水フェノール中,3
0℃で測定)が0.07〜0.17のEVOHが好まし
く使用される。
In the present invention, the degree of polymerization of EVOH is not particularly limited, but the intrinsic viscosity (15% by weight in water-containing phenol, 3%
EVOH of 0.07-0.17 (measured at 0 ° C.) is preferably used.

この発明で使用できるポリアミドはナイロン6,ナイロ
ン610,ナイロン12,などがあるが,特にEVOH
との相溶性及び成形温度を下げる点でナイロン6ベース
の共重合体,例えば6/66共重合体,6/12共重合
体,66/610/6共重合体などが好ましい。本発明
の特徴は,特定の末端基変性を行ったポリアミドを使用
することであり,アミノ末端基が8×10-5当量/g以
上で,且つカルボキシル末端基が3×10-5当量/g以
下であることが必要である。このような末端基の条件を
満足しないポリアミドを用いてEVOHと配合すると,
成形時に溶融粘度が増加し,長時間にわたる連続成形が
困難となる。このような末端基を有するポリアミドを得
る方法としては公知の方法が適用でき,例えば,ヘキサ
メチレンジアミンのような脂肪族ジアミンやメタキシレ
ンジアミンのような芳香族ジアミン等のジアミンを重合
時に添加することにより得られる。
Polyamides that can be used in this invention include nylon 6, nylon 610, nylon 12, etc., but especially EVOH
A nylon 6-based copolymer, for example, a 6/66 copolymer, a 6/12 copolymer, a 66/610/6 copolymer, or the like is preferable from the viewpoint of compatibility with and a decrease in molding temperature. The feature of the present invention is to use a polyamide modified with a specific end group, wherein the amino end group is 8 × 10 −5 equivalent / g or more and the carboxyl end group is 3 × 10 −5 equivalent / g. It must be: When blended with EVOH using a polyamide that does not satisfy the conditions of such end groups,
The melt viscosity increases during molding, making continuous molding difficult for a long time. As a method for obtaining a polyamide having such an end group, a known method can be applied. For example, addition of a diamine such as an aliphatic diamine such as hexamethylenediamine or an aromatic diamine such as metaxylenediamine at the time of polymerization. Is obtained by

本発明で用いられるポリアミドの重合度については,相
対粘度が2.1〜3.5,より好ましくは,2.2〜
3.2の範囲のものが使用される。相対粘度の測定方法
はJIS K-6810の4.4.1硫酸溶液による方法で測定さ
れる。硫酸濃度98%、温度25℃である。
Regarding the degree of polymerization of the polyamide used in the present invention, the relative viscosity is 2.1 to 3.5, more preferably 2.2.
Those in the range 3.2 are used. The relative viscosity is measured according to JIS K-6810 4.4.1 sulfuric acid solution. The sulfuric acid concentration is 98% and the temperature is 25 ° C.

本発明のような末端基にするためには,あまり相対粘度
の高いものは重合が困難であり,また,あまり相対粘度
が低いとEVOHと配合した場合に目的とする耐ピンホ
ール性あるいは耐衝撃性の改良が達成されない。
In order to obtain the terminal group as in the present invention, it is difficult to polymerize one having a relatively high relative viscosity, and when the relative viscosity is too low, the desired pinhole resistance or impact resistance when blended with EVOH. No improvement in sex is achieved.

この発明の樹脂組成物は,前述のEVOH100重量部
と,前述のポリアミド5150重量部,好ましくは10
〜100重量部とを,ポリマー成分として含有している
エチレン系共重合体ケン化物の樹脂組成物である。
The resin composition of this invention comprises 100 parts by weight of the above EVOH and 5150 parts by weight of the above polyamide, preferably 10 parts by weight.
The resin composition is a saponified ethylene-based copolymer containing 100 to 100 parts by weight as a polymer component.

この発明の樹脂組成物において,ケン化物に対するポリ
アミドの使用割合があまりに小さ過ぎると,そのような
樹脂組成物から形成された成形物の耐ピンホール性ある
いは耐衝撃性などの機械的性質が劣ったままであり改良
されないので適当ではなく,また,ケン化物に対するポ
リアミドの使用割合があまりに大きくなり過ぎると,そ
のような樹脂組成物から形成された成形物のガスバリヤ
ー性,剛性などが不十分となるので適当ではない。
In the resin composition of the present invention, if the ratio of the polyamide to the saponified product is too small, the molded product formed from such a resin composition may have poor mechanical properties such as pinhole resistance or impact resistance. It is not suitable because it is not improved, and if the proportion of polyamide used relative to the saponified product becomes too large, the gas barrier property, rigidity, etc. of the molded product formed from such a resin composition become insufficient. Not suitable.

この発明の樹脂組成物の調製法は,特に限定されず,通
常の公知の方法である『前記ケン化物とポリアミドとを
混合する方法』で行うことができる。
The method for preparing the resin composition of the present invention is not particularly limited, and the resin composition can be prepared by the commonly known method "method of mixing the saponified product with polyamide".

すなわち,前記ケン化物とポリアミドとの公知の混合方
法としては,例えば,前記ケン化物とポリアミドとを,
ペレット,粉末などの状態で均一に混合し,次いで,押
出混練機で溶融混練してペレット化して,そのペレット
を成形に使用する方法,あるいは,前記ケン化物とポリ
アミドとのペレット,粉末などを均一に混合して,その
混合物を直接,フィルム成形機や射出成形機に供給し,
その成形機内で混練しながら成形する方法などが適当で
ある。
That is, as a known mixing method of the saponified product and the polyamide, for example, the saponified product and the polyamide are
Pellet, powder, etc. are mixed uniformly, then melt-kneaded with an extrusion kneader to pelletize, and the pellet is used for molding, or pellets, powder, etc. of the saponified product and polyamide are uniformly mixed. And the mixture is directly supplied to a film molding machine or an injection molding machine,
A method of molding while kneading in the molding machine is suitable.

この発明の樹脂組成物をフィルム,容器,射出成形品な
どにするには,通常の押出し成形法,射出成形法が適用
可能であり,それらの成形において,長時間にわたりゲ
ル化物の発生がなく,安定した連続成形が可能である。
In order to make the resin composition of the present invention into a film, a container, an injection-molded product, etc., a usual extrusion molding method or injection molding method can be applied. Stable continuous molding is possible.

この発明の樹脂組成物からなるフィルム,シートなど
は,ガスバリヤー性,耐ピンホール性が優れていると共
に,透明性,耐薬品性なども保持しており,利用価値が
高い。さらにこの発明の樹脂組成物からなる射出成形品
は,剛性,耐熱性,耐衝撃性が優れていると共に,耐摩
耗特性,耐薬品性なども優れており,エンジニアリング
プラスチックスとして各種機能部品に使用できる。
Films, sheets, etc. made of the resin composition of the present invention are excellent in gas barrier properties and pinhole resistance, and at the same time, have transparency, chemical resistance, etc., and are highly useful. Furthermore, the injection-molded product made of the resin composition of the present invention has excellent rigidity, heat resistance and impact resistance, as well as excellent wear resistance and chemical resistance, and is used as engineering plastics for various functional parts. it can.

なお,この発明の樹脂組成物には,他の成分,例えば,
顔料,熱安定剤,酸化防止剤,耐候剤,結晶化促進剤,
滑剤,充填剤,可塑剤などを適当な量添加したものも含
まれる。特に,ガラス繊維を充填したものは,剛性,耐
クリープ性,耐熱性が高いため射出成形品として有用で
ある。
The resin composition of the present invention has other components, for example,
Pigment, heat stabilizer, antioxidant, weathering agent, crystallization accelerator,
It also includes those to which an appropriate amount of lubricants, fillers, plasticizers, etc. are added. In particular, those filled with glass fiber are useful as injection molded products because of their high rigidity, creep resistance and heat resistance.

〔実施例〕〔Example〕

以下に実施例および比較例を挙げてこの発明の樹脂組成
物をさらに具体的に示す。各実施例または比較例におけ
るフィルムの物性値の測定法は,次に述べる方法に従っ
て測定した。
Hereinafter, the resin composition of the present invention will be described more specifically with reference to Examples and Comparative Examples. The method for measuring the physical properties of the film in each Example or Comparative Example was measured according to the methods described below.

(1) 酸素透過度 20℃,絶乾状態の条件で,酸素ガス透過率測定装置
(モダンコントロール社製,OXYTRAN−100型)を用
いて測定した。
(1) Oxygen permeability Measured using an oxygen gas permeability measuring device (Modern Control Co., OXYTRAN-100 type) under conditions of 20 ° C. and absolutely dry condition.

(2) 耐ピンホール性 23℃,絶乾状態で,ASTM D−882に準じて引
取方向(M.D.)の引張試験を行った。その引張弾性
率および伸びを耐ピンホール性の尺度とした。すなわ
ち,前記の試験において,引張弾性率が低い程,また,
伸び率が大きい程,耐ピンホール性が良好であると評価
される。
(2) Pinhole resistance A tensile test was performed in the take-up direction (MD) according to ASTM D-882 in an absolutely dry state at 23 ° C. The tensile modulus and elongation were used as a measure of pinhole resistance. That is, in the above test, the lower the tensile modulus is,
The higher the elongation, the better the pinhole resistance.

また,以下の実施例および比較例における相対粘度の測
定法は先に示したJISK−6810(硫酸溶液による
方法、硫酸濃度98%、温度25℃)により,アミノ末
端基およびカルボキシ末端基の測定法は,Waltz,J.E.An
al Chem 19,448(1947)によった。アミノ末端基に
ついては試料をフェノール・メタノール混合溶液に溶解
し,メチルオレンジキシレンシアノールFF指示薬を用
いて で中和滴定する事により求め,カルボキシ末端基につい
ては,試料を熱ベンジルアルコールに溶解し,フェノー
ルフタレイン指示薬を用いて 水溶液で中和滴定する事により求めた。
Moreover, the measuring method of the relative viscosity in the following Examples and Comparative Examples is the measuring method of the amino terminal group and the carboxy terminal group according to JISK-6810 (method using sulfuric acid solution, sulfuric acid concentration 98%, temperature 25 ° C.) described above. Is Waltz, JEAn
al Chem 19 , 448 (1947). For amino end groups, dissolve the sample in a phenol / methanol mixed solution and use a methyl orange xylene cyanol FF indicator. The carboxy terminal group was dissolved in hot benzyl alcohol and the phenolphthalein indicator was used. It was determined by neutralization titration with an aqueous solution.

実施例1 エチレンモノマーに基づく反復単位Iを38モル%含有
しており,ケン化度が99%,極限粘度0.14,融点
173℃である『エチレン−酢酸ビニル共重合体のケン
化物(EVOH)』100重量部に,相対粘度2.7,
アミノ末端基9.7×10-5当量/g,カルボキシ末端基
2.0×10-5当量/gのナイロン6(A)43重量部を
ペレット状でブレンドした。その混合物を押出し成形機
(T−ダイ押出し成形機,スクリュー径が40mmであ
る)に供給し,250℃で溶融押出しを行い,前記EVOH
とナイロン6(A)とのポリマー成分からなる樹脂組成物
のフィルム状体を押出し,次いで表面温度が70℃であ
るキャスティングドラム上で冷却固化させて厚さ約50
μのフィルムを成形した。このフィルムについて次の物
性評価を行った。
Example 1 An ethylene-vinyl acetate copolymer saponified product (EVOH) containing 38 mol% of repeating unit I based on an ethylene monomer, having a saponification degree of 99%, an intrinsic viscosity of 0.14 and a melting point of 173 ° C. ) ”100 parts by weight, relative viscosity 2.7,
43 parts by weight of nylon 6 (A) having amino terminal groups of 9.7 × 10 −5 equivalent / g and carboxy terminal groups of 2.0 × 10 −5 equivalent / g were blended in a pellet form. The mixture is supplied to an extrusion molding machine (T-die extrusion molding machine, screw diameter is 40 mm) and melt-extruded at 250 ° C.
A film of a resin composition consisting of a polymer component of nylon and nylon 6 (A) is extruded and then cooled and solidified on a casting drum having a surface temperature of 70 ° C. to have a thickness of about 50.
A film of μ was formed. The following physical properties of this film were evaluated.

尚,成形時のゲル化挙動については,成形温度を250
℃とゲル化に対して,厳しい条件にし,フィルムにゲル
が発生するまでの時間を測定した。
Regarding the gelling behavior during molding, the molding temperature should be 250
The conditions were set to be severe against ℃ and gelation, and the time until gel formation on the film was measured.

これらの結果を第1表に示す。The results are shown in Table 1.

前述の製膜において,使用した樹脂組成物はゲル化を起
こしにくく,250℃の高温成形でも成形10時間後で
もゲル化物の発生がなく,また,前述の製膜によって得
られたフィルムは,耐ピンホール性が著しく改良されて
おり,さらにガスバリヤー性も良好であった。
In the above-mentioned film formation, the resin composition used does not easily cause gelation, no gelation occurs even at 250 ° C. high temperature molding or 10 hours after molding, and the film obtained by the above film formation is The pinhole property was remarkably improved, and the gas barrier property was also good.

実施例2 ナイロン6(A)の代わりに,6/66共重合体(A)〔ナイ
ロン6の構成単位とナイロン66の構成単位とのモル比
(6/66)が85/15で,融点が195℃,相対粘
度が2.8で,アミノ末端基が9.0×10-5当量/g
で,カルボキシ末端基が2.2×10-5当量/gであ
る〕を43重量部使用したほかは,実施例1と同様にし
て,フィルムを成形した。
Example 2 Instead of nylon 6 (A), 6/66 copolymer (A) [molar ratio (6/66) of the structural units of nylon 6 and the structural unit of nylon 66 was 85/15, and the melting point was 195 ° C., relative viscosity 2.8, amino end groups 9.0 × 10 −5 equivalent / g
Then, a film was formed in the same manner as in Example 1 except that 43 parts by weight of carboxy terminal group was 2.2 × 10 −5 equivalent / g.

その結果を第1表に示す。The results are shown in Table 1.

得られたフィルムは,ガスバリヤー性および耐ピンホー
ルが共に良好であり,さらに製膜時にゲル化物の発生も
なかった。
The obtained film was excellent in both gas barrier property and pinhole resistance, and gelation was not generated during film formation.

実施例3 実施例2の6/66共重合体(A)の使用量を11重量部
に変えたほかは,実施例1と同様にして,フィルムを成
形した。
Example 3 A film was formed in the same manner as in Example 1 except that the amount of 6/66 copolymer (A) used in Example 2 was changed to 11 parts by weight.

実施例4 実施例2の6/66共重合体(A)の使用量を100重量
部に変えたほかは,実施例1と同様にして,フィルムを
成形した。
Example 4 A film was formed in the same manner as in Example 1 except that the amount of the 6/66 copolymer (A) used in Example 2 was changed to 100 parts by weight.

これらの結果を第1表に示すが,実施例3及び実施例4
とも良好な結果が得られた。
These results are shown in Table 1 and are shown in Example 3 and Example 4.
Both were good results.

実施例5 ポリアミドとして6/12共重合体(A)〔ナイロン6の
構成単位とナイロン12の構成単位とのモル比(6/1
2)が80/20で,融点が196℃,相対粘度が2.
5,アミノ末端基が10.5×10-5当量/g,カルボ
キシ末端基が2.1×10-5当量/gである〕を43重
量部使用したほかは,実施例1と同様にして,フィルム
を成形した。
Example 5 As a polyamide, a 6/12 copolymer (A) [a molar ratio of a structural unit of nylon 6 and a structural unit of nylon 12 (6/1
2) is 80/20, melting point is 196 ° C., and relative viscosity is 2.
5, amino end groups are 10.5 × 10 −5 equivalent / g and carboxy end groups are 2.1 × 10 −5 equivalent / g] in the same manner as in Example 1 except that 43 parts by weight are used. , The film was formed.

その結果を第1表に示す。The results are shown in Table 1.

得られたフィルムは,ガスバリヤー性および耐ピンホー
ル性が共に良好であり,成形10時間後でもゲル化物は
発生しなかった。
The obtained film was excellent in both gas barrier property and pinhole resistance, and no gelled product was generated even after 10 hours from molding.

比較例1 ポリアミドを全く使用しなかったほかは,実施例1と同
様にして,フィルムを成形した。
Comparative Example 1 A film was formed in the same manner as in Example 1 except that no polyamide was used.

その結果を第1表に示す。The results are shown in Table 1.

前述のようにして得られたフィルムは,ガスバリヤー性
が良好であるが,固くて伸びが小さいため耐ピンホール
性が劣っている。
The film obtained as described above has a good gas barrier property, but is poor in pinhole resistance because it is hard and has a small elongation.

比較例2 ポリアミドとして,相対粘度2.9,アミノ末端基4.
6×10-5当量/g,カルボキシ末端基5.3×10-5
当量/gのナイロン6(B)を43重量部使用したほか
は,実施例1と同様にして,フィルムを成形した。
Comparative Example 2 A polyamide having a relative viscosity of 2.9 and an amino end group of 4.
6 × 10 -5 equivalent / g, carboxy end group 5.3 × 10 -5
A film was formed in the same manner as in Example 1 except that 43 parts by weight of nylon 6 (B) having an equivalent weight / g was used.

比較例3 ポリアミドとして,6/66共重合体(B)〔ナイロン6
の構成単位とナイロン66の構成単位とのモル比(6/
66)が85/15で,融点が195℃,相対粘度が2.
7で,アミノ末端基が6.8×10-5当量/g,カルボ
キシ末端基が5.4×10-5当量/g〕を43重量部使
用したほかは,実施例1と同様にして,フィルムを成形
した。
Comparative Example 3 As polyamide, 6/66 copolymer (B) [nylon 6
Molar ratio of the structural unit of 6 to the structural unit of nylon 66 (6 /
66) is 85/15, the melting point is 195 ° C., and the relative viscosity is 2.
7, the amino terminal group was 6.8 × 10 −5 equivalent / g and the carboxy terminal group was 5.4 × 10 −5 equivalent / g] in the same manner as in Example 1 except that 43 parts by weight was used. A film was formed.

比較例4 ポリアミドとして,6/66共重合体(C)〔ナイロン6
の構成単位とナイロン66の構成単位とのモル比(6/
66)が85/15で,融点が195℃,相対粘度が2.
6で,アミノ末端基が8.5×10-5当量/g,カルボ
キシ末端基5.1×10-5当量/g〕を43重量部使用
したほかは,実施例1と同様にして,フィルムを成形し
た。
Comparative Example 4 As polyamide, 6/66 copolymer (C) [nylon 6
Molar ratio of the structural unit of 6 to the structural unit of nylon 66 (6 /
66) is 85/15, the melting point is 195 ° C., and the relative viscosity is 2.
6, the amino terminal group was 8.5 × 10 −5 equivalent / g, and the carboxyl terminal group was 5.1 × 10 −5 equivalent / g] in the same manner as in Example 1 except that 43 parts by weight was used. Was molded.

比較例5 ポリアミドとして,6/12共重合体(B)〔ナイロン6
の構成単位とナイロン12の構成単位とのモル比(6/
12)が80/20で,融点が196℃,相対粘度が2.
6,アミノ末端基が6.7×10-5当量/g,カルボキ
シ末端基が3.1×10-5当量/g〕を43重量部使用
したほかは,実施例1と同様にして,フィルムを成形し
た。
Comparative Example 5 As a polyamide, a 6/12 copolymer (B) [nylon 6
Molar ratio of the structural unit of 6 to that of nylon 12 (6 /
12) 80/20, melting point 196 ° C, relative viscosity 2.
6, amino terminal group was 6.7 × 10 −5 equivalent / g, and carboxy terminal group was 3.1 × 10 −5 equivalent / g] in the same manner as in Example 1 except that 43 parts by weight was used. Was molded.

これらの結果を表1に示したが,比較例2,3,4,5
とも成形1〜2時間後にゲルが発生し,さらに成形を続
けると製膜が困難となった。
These results are shown in Table 1, and Comparative Examples 2, 3, 4, 5
In both cases, gel was generated 1 to 2 hours after molding, and film formation became difficult when molding was continued.

比較例6 実施例2の6/66共重合体(A)の使用量を3重量部に
変えたほかは,実施例1と同様にして,フィルムを成形
した。
Comparative Example 6 A film was formed in the same manner as in Example 1 except that the amount of the 6/66 copolymer (A) used in Example 2 was changed to 3 parts by weight.

その結果を表1に示すが,前述のようにして得られたフ
ィルムは,耐ピンホール性がほとんど改良されていなか
った。
The results are shown in Table 1. The film obtained as described above had almost no improvement in pinhole resistance.

比較例7 実施例2の6/66共重合体(A)の使用量を230重量部に
変えたほかは,実施例1と同様にして,フィルムを成形
した。
Comparative Example 7 A film was formed in the same manner as in Example 1 except that the amount of the 6/66 copolymer (A) used in Example 2 was changed to 230 parts by weight.

その結果を表1に示すが,前述のようにして得られたフ
ィルムは,ガスバリヤー性が著しく悪化していた。
The results are shown in Table 1, and the gas barrier properties of the film obtained as described above were significantly deteriorated.

比較例8 ポリアミドとして,6/66共重合体(D)〔ナイロン6
の構成単位とナイロン66の構成単位とのモル比(6/
66)が85/15で,融点が195℃,相対粘度が2.
8で,アミノ末端基が2.2×10-5当量/g,カルボキ
シ末端基が95×10-5当量/g〕を43重量部使用したほ
かは,実施例1と同様にして,フィルム成形を行った
が,成形時にゲルが著しく発生し,製膜が困難となっ
た。
Comparative Example 8 As a polyamide, a 6/66 copolymer (D) [nylon 6
Molar ratio of the structural unit of 6 to the structural unit of nylon 66 (6 /
66) is 85/15, the melting point is 195 ° C., and the relative viscosity is 2.
In the same manner as in Example 1, except that 43 parts by weight of amino terminal group was 2.2 × 10 −5 equivalent / g and carboxy terminal group was 95 × 10 −5 equivalent / g. However, gelling was remarkably generated during molding, and film formation became difficult.

実施例6 エチレンモノマーに基づく反復単位Iを38モル%含有
しており,ケン化度が99%,極限粘度0.11,融点
173℃であるEVOHにガラス繊維を25%配合した
もの100重量部に,6/66共重合体(A)43重量部をペ
レット状でブレンドした。その混合物を用いて射出成形
機により引張用試験片(ASTM D−638)及びア
イゾット衝撃試験片(ASTM D−256)をシリン
ダー温度250℃で成形した。射出成形を長時間行って
もゲル化物の発生がなかった。前述のようにして成形し
た試験片について,ASTM規格により測定を行った
が,引張破断点伸び16%,アイゾット衝撃強度(ノッ
チ付)9.4Kg・cm/cmと耐衝撃性は改良されていた。
Example 6 EVOH containing 38 mol% of repeating unit I based on an ethylene monomer, having a saponification degree of 99%, an intrinsic viscosity of 0.11, and a melting point of 173 ° C. was blended with 25% of glass fiber 100 parts by weight. Then, 43 parts by weight of 6/66 copolymer (A) was blended in the form of pellets. Using the mixture, a tensile test piece (ASTM D-638) and an Izod impact test piece (ASTM D-256) were molded by an injection molding machine at a cylinder temperature of 250 ° C. No gelation was observed even after injection molding for a long time. The test pieces molded as described above were measured according to the ASTM standard. The tensile break elongation was 16%, the Izod impact strength (notched) was 9.4 kg · cm / cm, and the impact resistance was improved. .

比較例9 ポリアミドを全く使用しなかったほかは,実施例6と同
様にして、試験片を射出成形した。この試験片について
測定を行ったが,破断点伸び9%,アイゾット衝撃強度
(ノッチ付)6.8Kg・cm/cmであった。
Comparative Example 9 A test piece was injection-molded in the same manner as in Example 6 except that no polyamide was used. The test piece was measured and found to have an elongation at break of 9% and an Izod impact strength (notched) of 6.8 kg · cm / cm.

比較例10 実施例の6/66共重合体(A)の代わりに,比較例3で
用いた6/66共重合体(B)43重量部を使用し,実施
例6と同様にして,試験片を射出成形した。成形100
ショット(成形開始約1時間後)あたりからゲル化物が
発生し始め,さらに成形を続けるとゲル化物のため成形
が困難となった。
Comparative Example 10 In the same manner as in Example 6, except that 43 parts by weight of 6/66 copolymer (B) used in Comparative Example 3 was used instead of 6/66 copolymer (A) of Example, a test was conducted. The pieces were injection molded. Molding 100
A gelled product started to be generated around a shot (about 1 hour after the start of molding), and when the molding was continued further, the molding became difficult because of the gelled product.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】エチレンモノマーに基づく反復単位(−CH
2−CH2−)を5〜50モル%有していると共に、ケン化
度が80%以上であるエチレンと酢酸ビニルとの共重合
体のケン化物100重量部と、相対粘度が2.1〜3.
5で,かつ、アミノ末端基が8×10-5当量/g以上で、
カルボキシ末端基が3×10-5当量/g以下であるアミノ
末端リッチの末端変性されたポリアミド5〜150重量
部とからなることを特徴とするエチレン系共重合体ケン
化物の樹脂組成物。
1. A repeating unit (—CH 2) based on an ethylene monomer.
2- CH 2 —) in an amount of 5 to 50 mol%, and 100 parts by weight of a saponified product of a copolymer of ethylene and vinyl acetate having a saponification degree of 80% or more, and a relative viscosity of 2.1. ~ 3.
5, and the amino end group is 8 × 10 −5 equivalent / g or more,
A resin composition of a saponified ethylene-based copolymer, which comprises 5 to 150 parts by weight of an amino-terminal rich terminal-modified polyamide having a carboxy terminal group of 3 × 10 −5 equivalent / g or less.
JP15229985A 1985-07-12 1985-07-12 Resin composition of saponified ethylene copolymer Expired - Lifetime JPH0611832B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP15229985A JPH0611832B2 (en) 1985-07-12 1985-07-12 Resin composition of saponified ethylene copolymer
US06/883,078 US4749744A (en) 1985-07-12 1986-07-08 Resin composition of saponified ethylenic copolymer
DE8686305302T DE3683974D1 (en) 1985-07-12 1986-07-10 PLASTIC COMPOSITION MADE OF SOAPED AETHYLENE COPOLYMER.
EP86305302A EP0214724B1 (en) 1985-07-12 1986-07-10 Resin composition of saponified ethylenic copolymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15229985A JPH0611832B2 (en) 1985-07-12 1985-07-12 Resin composition of saponified ethylene copolymer

Publications (2)

Publication Number Publication Date
JPS6213449A JPS6213449A (en) 1987-01-22
JPH0611832B2 true JPH0611832B2 (en) 1994-02-16

Family

ID=15537486

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Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPH0611832B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6222840A (en) * 1985-07-22 1987-01-31 Nippon Synthetic Chem Ind Co Ltd:The Resin composition
US4990562A (en) * 1987-08-24 1991-02-05 E. I. Du Pont De Nemours And Company Blends of ethylene vinyl alcohol copolymer and amorphous polyamide, and multilayer containers made therefrom
US5064716A (en) * 1989-01-26 1991-11-12 E. I. Du Pont De Nemours And Company Blends of ethylene vinyl alcohol copolymer and amorphous polyamide, and multilayer containers made therefrom
JP2008274059A (en) * 2007-04-27 2008-11-13 Nippon Synthetic Chem Ind Co Ltd:The Resin composition

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