JPH0788452B2 - Resin composition - Google Patents

Resin composition

Info

Publication number
JPH0788452B2
JPH0788452B2 JP3528487A JP3528487A JPH0788452B2 JP H0788452 B2 JPH0788452 B2 JP H0788452B2 JP 3528487 A JP3528487 A JP 3528487A JP 3528487 A JP3528487 A JP 3528487A JP H0788452 B2 JPH0788452 B2 JP H0788452B2
Authority
JP
Japan
Prior art keywords
ethylene
evoh
revoh
mol
olefin resin
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 - Fee Related
Application number
JP3528487A
Other languages
Japanese (ja)
Other versions
JPS63202638A (en
Inventor
潔 米津
明正 青山
健 守谷
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.)
Kuraray Co Ltd
Original Assignee
Kuraray Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kuraray Co Ltd filed Critical Kuraray Co Ltd
Priority to JP3528487A priority Critical patent/JPH0788452B2/en
Publication of JPS63202638A publication Critical patent/JPS63202638A/en
Publication of JPH0788452B2 publication Critical patent/JPH0788452B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Compositions Of Macromolecular Compounds (AREA)
  • Polymerisation Methods In General (AREA)

Description

【発明の詳細な説明】 A.産業上の利用分野 本発明はエチレン−ビニルアルコール系共重合体とオレ
フイン系樹脂の組成物において、混合分散性不良に基づ
くと推定される各種性能の低下を改善することにより、
各種の包装材料分野に極めて有用な樹脂組成物を提供す
ることにある。
DETAILED DESCRIPTION OF THE INVENTION A. Field of Industrial Application The present invention improves the deterioration of various performances presumed to be due to poor mixing and dispersibility in a composition of ethylene-vinyl alcohol copolymer and olefin resin. By doing
An object of the present invention is to provide a resin composition extremely useful in various packaging material fields.

B.従来の技術 従来、エチレン−ビニルアルコール系共重合体(EVOH)
とオレフイン系樹脂のブレンド物の利用については、そ
の両者の優れた性能を生かして、各種の技術が提案され
ている。例えば、オレフイン系樹脂の耐ガス透過性を改
良、または調節するためにEVOHをブレンドすること、あ
るいはオレフイン系農業用フイルムの保温性を改良する
ためにEVOHをブレンドすること、あるいはEVOHに柔軟
性、耐衝撃性を付与するためオレフイン系樹脂をブレン
ドすること、あるいはオレフイン系樹脂の耐溶剤性を改
良するためEVOHをブレンドすること、あるいはEVOHの各
種成形加工性を改良するためオレフイン系樹脂をブレン
ドすること、等が提案されている。
B. Conventional technology Conventionally, ethylene-vinyl alcohol copolymer (EVOH)
Various technologies have been proposed for the use of a blend of olefin resin and olefin resin by making use of the excellent performance of both. For example, blending EVOH to improve or adjust the gas permeation resistance of the olefin resin, or blend EVOH to improve the heat retention of the olefin polymer film, or flexible to EVOH, Blending olefin resin to impart impact resistance, blending EVOH to improve solvent resistance of olefin resin, or blending olefin resin to improve various moldability of EVOH. Have been proposed.

しかし、EVOHとオレフイン系樹脂は本来親和性が低く、
両者のブレンド物における分散性不良のためか、両者の
ブレンド物による成形物、フイルムはある種の機械的性
能が著しく損なわれたり、透明性が大きく低下して満足
な包装材料等を提供できない。
However, EVOH and olefin resin originally have low affinity,
Probably because of poor dispersibility in the blended product of both, the molded product and film made of the blended product of both are remarkably impaired in certain mechanical performance, or the transparency is greatly lowered, and a satisfactory packaging material or the like cannot be provided.

C.発明が解決しようとする問題点 本発明は前記の欠点、即ちEVOHとオレフイン系樹脂のブ
レンド物において、ある種の機械的性能を著しく損なう
ことなく、また透明性を大きく低下させることなく、両
者の性能を生かして有用な包装材料等に利用できる樹脂
組成物を提供するものである。
C. Problems to be Solved by the Invention The present invention has the above-mentioned drawbacks, that is, in a blend of EVOH and an olefin resin, without significantly impairing some mechanical performance and without significantly reducing transparency, It is intended to provide a resin composition that can be utilized as a useful packaging material and the like by making the best use of the performance of both.

D.問題点を解決するための手段 本発明者らは鋭意研究を重ねた結果、EVOHとオレフイン
系樹脂のブレンド物において、末端にRS基(但しRは炭
素数2〜30の炭化水素、Sは硫黄原子)を有するエチレ
ン−ビニルアルコール系共重合体(REVOH)、または該
共重合体とEVOHとの混合物を用いることにより、EVOHと
オレフイン系樹脂の混合分散性不良に基づくと推定され
る前記の欠点が改良されることを見出した。
D. Means for Solving the Problems As a result of intensive studies by the present inventors, in a blend of EVOH and an olefin resin, an RS group at the terminal (where R is a hydrocarbon having 2 to 30 carbon atoms, S Is a sulfur atom) having an ethylene-vinyl alcohol-based copolymer (REVOH) or a mixture of the copolymer and EVOH, which is presumed to be based on poor mixing dispersibility of EVOH and olefin resin. It has been found that the drawbacks of are improved.

E.発明のより詳細な説明 本発明のREVOHとは前述した通り、末端にRS基(但しR
は炭素数4〜30の炭化水素、Sは硫黄原子)を有するエ
チレン−ビニルアルコール系共重合体であり、Rを具体
的に例示すると、i−ブチル、t−ブチル、n−ヘキシ
ル、n−オクチル、n−デシル、n−ドテシル、n−テ
トラデシル、n−ヘキサデシル、n−オクタデシル、n
−イコシル等である。このうち特に炭素数6〜18のもの
が好適に用いられる。
E. More Detailed Description of the Invention As described above, the REVOH of the present invention has a terminal RS group (provided that R
Is an ethylene-vinyl alcohol copolymer having a hydrocarbon having 4 to 30 carbon atoms, S is a sulfur atom), and specific examples of R are i-butyl, t-butyl, n-hexyl, n- Octyl, n-decyl, n-dothesyl, n-tetradecyl, n-hexadecyl, n-octadecyl, n
-Icosyl and the like. Of these, those having 6 to 18 carbon atoms are particularly preferably used.

REVOHは一般に以下の方法で製造される。即ち、エチレ
ン、酢酸ビニル、さらに要すれば少量の他のオレフイン
系不飽和化合物のラジカル共重合を行う際に、R-SHで表
わされるメルカプタンを存在させる、いわゆる連鎖移動
法によりRS基を末端(片末端)に導入せしめたエチレン
−酢酸ビニル系共重合体を製造し、これを常法によりケ
ン化することによつて製造することができる。このよう
にして得られるREVOHの全片末端中のRS基の含有量は30
モル%以上、好ましくは40モル%以上である。この場
合、末端のRS基はRの如何にかかわらず、RS基1個をポ
リマー成分のモノマー1個と考える。
REVOH is generally manufactured by the following method. That is, when performing radical copolymerization of ethylene, vinyl acetate, and optionally a small amount of other olefinic unsaturated compound, the mercaptan represented by R-SH is present, and the RS group is terminated by a so-called chain transfer method ( It can be produced by producing an ethylene-vinyl acetate copolymer introduced at one end) and saponifying it by a conventional method. The content of RS groups in all terminals of REVOH thus obtained is 30
It is at least mol%, preferably at least 40 mol%. In this case, one RS group is considered to be one monomer of the polymer component regardless of whether the terminal RS group is R or not.

REVOH、およびこれと混合使用されるEVOHのエチレン含
有率は20〜60モル%、好適には25〜55モル%であり、酢
酸ビニル成分のケン化度は90モル%以上が好ましい。エ
チレン含有率が20モル%未満では成形性が悪化し、エチ
レン含有率が60モル%を越えると、またケン化度が90モ
ル%未満になると、EVOH本来の特性である耐ガス透過
性、耐油性、耐溶剤性、保温性等が悪化し好ましくな
い。
The ethylene content of REVOH and EVOH mixed with it is 20 to 60 mol%, preferably 25 to 55 mol%, and the saponification degree of the vinyl acetate component is preferably 90 mol% or more. When the ethylene content is less than 20 mol%, the moldability deteriorates. When the ethylene content exceeds 60 mol%, and when the saponification degree is less than 90 mol%, the EVOH's original characteristics of gas permeation resistance and oil resistance. Properties, solvent resistance, heat retention and the like are deteriorated, which is not preferable.

REVOHはその製造方法から、重合度が低下するのは避け
得ないが、重合度の低いREVOHを配合して、要求性能が
満たされる場合は、REVOHのみの配合で充分である。し
かしながら重合度の低いREVOHのみをオレフイン系樹脂
に配合しても要求性能が満されない場合、たとえばより
優れた耐衝撃強度などを付与したい場合は、これを防ぐ
ために、REVOHに重合度の高いEVOHを混合使用するのが
望ましい。この場合、両者のエチレン含有率、ケン化度
は上記範囲内に任意に選びうるが、エチレン含有率ケン
化度ともお互いに近接していることが好ましく、例えば
エチレン含有率の差が20モル%以下、ケン化度の差が5
モル%以下であることが好ましい。REVOHのメルトイン
デツクス(MI)g/10分(2160gの荷重下、190℃で測定)
は0.1〜500の範囲から選ばれ、またEVOHのMIは0.1〜50
の範囲から選ばれる。
From the manufacturing method of REVOH, it is inevitable that the degree of polymerization will decrease, but if REVOH having a low degree of polymerization is blended and the required performance is satisfied, blending of REVOH alone is sufficient. However, if the required performance is not satisfied even if only REVOH having a low degree of polymerization is blended with the olefin resin, for example, if it is desired to impart better impact strength, then EVV with a high degree of polymerization is added to REVOH to prevent this. It is desirable to use a mixture. In this case, the ethylene content and saponification degree of both can be arbitrarily selected within the above range, but the ethylene content and the saponification degree are preferably close to each other, for example, the difference in ethylene content is 20 mol%. Below, the difference in saponification degree is 5
It is preferably not more than mol%. REVOH melt index (MI) g / 10 minutes (measured at 190 ° C under a load of 2160 g)
Is selected from the range of 0.1 to 500, and MI of EVOH is 0.1 to 50.
Selected from the range.

EVOHのREVOHへの混合割合は、その用途により任意に選
びうるものであり、驚くべきことに、EVOHにわずか5〜
10%のREVOHを含むだけでオレフイン樹脂との分散性不
良に基づくと推定される性能低下を防止できる。この場
合、あらかじめオレフイン樹脂とREVOHを混合分散し、
この組成物をEVOHにブレンドする方法が著しく効果的で
ある場合がある。
The mixing ratio of EVOH to REVOH can be arbitrarily selected depending on the application, and surprisingly, EVOH has a mixing ratio of only 5 to 5.
Only by including 10% of REVOH, it is possible to prevent the performance deterioration estimated to be based on the poor dispersibility with the olefin resin. In this case, olefin resin and REVOH are mixed and dispersed beforehand,
The method of blending this composition with EVOH can be extremely effective.

REVOH、またはREVOHとEVOHの混合物(A)とブレンド使
用されるオレフイン系樹脂(B)としては、その用途に
より任意に選びうるが、例えば、低密度、中密度、高密
度ポリエチレン、ポリプロピレン、エチレン−プロピレ
ン共重合体、プロピレン−ブテン−1共重合体、エチレ
ン−酢酸ビニル共重合体、イオン架橋オレフイン共重合
体、あるいはこれらの二種以上の混合物が例示される。
(A)と(B)の混合割合は、その用途によつて適切に
決定されるものであり、その重量比で95:5ないし5:95の
範囲内で任意に選びうる。例えば、ポリエチレン容器の
耐ガス透過性、耐溶剤性を改良する目的であれば、
(A):(B)は5:95ないし45:55の範囲内で主に使用
され、EVOHに耐衝撃性、柔軟性を付与する目的であれ
ば、(A):(B)は55:45ないし95:5の範囲内で主に
使用される。ブレンド方法には、バンバリミキサーによ
る方法、単軸あるいは二軸スクリユー押出機による溶融
ブレンド方法など公知の方法が採用できる。またこのブ
レンドの際に、本発明の作用効果が阻害されない範囲で
他の添加剤、例えば酸化防止剤、紫外線吸収剤、滑剤、
可塑剤、帯電防止剤、着色剤等を配合できる。
The olefin resin (B) to be blended with REVOH or a mixture of REVOH and EVOH (B) can be arbitrarily selected according to its application, and examples thereof include low density, medium density, high density polyethylene, polypropylene, ethylene- Examples thereof include a propylene copolymer, a propylene-butene-1 copolymer, an ethylene-vinyl acetate copolymer, an ion-crosslinked olefin copolymer, or a mixture of two or more of these.
The mixing ratio of (A) and (B) is appropriately determined depending on the application, and can be arbitrarily selected within the range of 95: 5 to 5:95 by weight ratio. For example, for the purpose of improving the gas permeation resistance and solvent resistance of a polyethylene container,
(A): (B) is mainly used within the range of 5:95 to 45:55, and for the purpose of imparting impact resistance and flexibility to EVOH, (A): (B) is 55: Mainly used in the range of 45 to 95: 5. As the blending method, known methods such as a Banbury mixer method and a melt blending method using a single-screw or twin-screw extruder can be adopted. Further, in the case of this blending, other additives such as an antioxidant, an ultraviolet absorber, a lubricant, within a range that does not impair the action and effect of the present invention,
A plasticizer, an antistatic agent, a coloring agent and the like can be added.

このようにして得られた本発明の樹脂組成物は、周知の
溶融成形方法で容易に成形可能であり、フイルム、シー
ト、チユーブ、ボトルなど任意の成形品に成形すること
ができる。また他の熱可塑性樹脂、例えばポリエチレ
ン、ポリプロプレン、ポリエチレンテレフタレート、ポ
リアミド、ポリスチレン等との多層積層体としても用い
られ、多層共押出、共射出、押出コーテイング等公知の
方法で成形され、各種包装材料等に使用される。多層積
層体としては、本発明の樹脂組成物をE、熱可塑性樹脂
をPとするとき、P/E、P/E/P、P/E/P/E/P、E/P/E、E/P/
E/Pなどの層構成があげられる。この場合各層間には必
要に応じ層間接着剤を設けることもできる。
The resin composition of the present invention thus obtained can be easily molded by a well-known melt molding method, and can be molded into an arbitrary molded product such as a film, a sheet, a tube or a bottle. It is also used as a multi-layer laminate with other thermoplastic resins such as polyethylene, polypropylene, polyethylene terephthalate, polyamide, polystyrene, etc., and is formed by a known method such as multi-layer coextrusion, co-injection, extrusion coating, and various packaging materials. Used for etc. As the multilayer laminate, when the resin composition of the present invention is E and the thermoplastic resin is P, P / E, P / E / P, P / E / P / E / P, E / P / E, E / P /
The layer structure such as E / P can be mentioned. In this case, an interlayer adhesive may be provided between the layers, if necessary.

以下実施例をあげて本発明をさらに詳しく説明するが、
これらの実施例によつて本発明は何ら限定されるもので
はない。
Hereinafter, the present invention will be described in more detail with reference to Examples.
The present invention is not limited to these examples.

F.実施例 実施例1、対照例1 エチレン含有率29モル%、ケン化度99モル%で、その片
末端の45モル%にn−ドデシルチイル基を有するメルト
インデツクス10のエチレン−ビニルアルコールを20重量
部と、低密度ポリエチレン(密度0.921、メルトインデ
ツクス1.5)80重量部を混合後、一軸フルフライト型ス
クリユーを有する押出機に供給して温度220℃でペレツ
ト化し、ついでこのペレツトをT−ダイを備えた押出成
膜機に供給して、以下の条件で厚み40μのフイルムを製
造した。
F. Examples Example 1, Control Example 1 Ethylene-vinyl alcohol of melt index 10 having an ethylene content of 29 mol% and a saponification degree of 99 mol% and having n-dodecylthiyl group at 45 mol% of one end thereof. After mixing 20 parts by weight and 80 parts by weight of low-density polyethylene (density 0.921, melt index 1.5), the mixture is supplied to an extruder having a uniaxial full flight type screw, pelletized at a temperature of 220 ° C., and then the pellet is T- The film was supplied to an extrusion film-forming machine equipped with a die to produce a film having a thickness of 40 μm under the following conditions.

押 出 機:40mm径 スクリユー:フルフライト型、L/D=28、圧縮比4.0 ダ イ :T−ダイ300mm巾 成膜温度 :シリンダー、180℃、210℃、220℃ ダイ、220℃ 引取速度 :10m/分 対照例として、エチレン含有率29モル%、ケン化度99モ
ル%、メルトインデツクス10の通常の末端を有するエチ
レン−ビニルアルコールを用いて、上記と同様にポリエ
チレンと混合操作を行つて樹脂組成物の40μのフイルム
を得た。両者のフイルムついて主な物性を測定した結果
を第1表に示す。引張破断強伸度、透明性の点で顕著な
差が認められた。
Extruder: 40mm diameter screw: Full flight type, L / D = 28, compression ratio 4.0 dy: T-die 300mm width Film forming temperature: Cylinder, 180 ℃, 210 ℃, 220 ℃ die, 220 ℃ Collection speed: As a control example, ethylene-vinyl alcohol having an ethylene content of 29 mol%, a saponification degree of 99 mol% and a normal end of melt index 10 was used, and a mixing operation with polyethylene was performed in the same manner as above. A 40 μ film of the resin composition was obtained. Table 1 shows the results of measuring the main physical properties of both films. Significant differences were observed in terms of tensile strength at break and elongation and transparency.

実施例2〜5、対照例2〜5 実施例1で用いたREVOHを使用し、各種オレフイン系樹
脂との組成物のフイルムを実施例1と同様に製造した。
また対照として対照例1で用いたEVOHを使用して、各種
オレフイン系樹脂との組成物のフイルムを得て実施例1
と同様に物性を比較した。結果を第2表に示す。
Examples 2 to 5 and Control Examples 2 to 5 Using REVOH used in Example 1, films of compositions with various olefin resins were produced in the same manner as in Example 1.
As a control, EVOH used in Comparative Example 1 was used to obtain a film of a composition with various olefin resins, and Example 1 was used.
Similarly, the physical properties were compared. The results are shown in Table 2.

実施例6、対照例6 エチレン含有率34モル%、ケン化度97モル%で、その片
末端の86モル%にn−オクタデシルチイル基を有するメ
ルトインデツクス65のエチレン−ビニルアルコール20重
量部と、酢酸ビニル28重量%のエチレン−酢酸ビニル共
重合体80重量部を混合し、あらかじめペレツト化してお
く。次にエチレン含有率34モル%、ケン化度99モル%、
メルトインデツクス2.6の通常の末端を有するエチレン
−ビニルアルコールのペレツト70重量部に、前記混合ペ
レツト30重量部を混合し、実施例1と同装置を用いて厚
さ60μのフイルムを得た。
Example 6, Control Example 6 20 parts by weight of ethylene-vinyl alcohol in a melt index 65 having an ethylene content of 34 mol% and a saponification degree of 97 mol% and having an n-octadecylthiyl group at 86 mol% of one end thereof. And 28 parts by weight of vinyl acetate and 80 parts by weight of an ethylene-vinyl acetate copolymer are mixed and pelletized in advance. Next, ethylene content 34 mol%, saponification degree 99 mol%,
30 parts by weight of the above mixed pellets were mixed with 70 parts by weight of ethylene-vinyl alcohol pellets having a melt index of 2.6 and having a normal end, and a film having a thickness of 60 .mu.m was obtained using the same apparatus as in Example 1.

対照例として、上記の通常のエチレン−ビニルアルコー
ルのペレツト76重量部に、上記エチレン−酢酸ビニル共
重合体ペレツト24重量部を混合し、同様に厚さ60μのフ
イルムを得た。
As a control, 76 parts by weight of the above-mentioned usual ethylene-vinyl alcohol pellets were mixed with 24 parts by weight of the above ethylene-vinyl acetate copolymer pellets to obtain a film having a thickness of 60 .mu.m.

両者のフイルムの物性を測定した結果、衝撃強度、ヘイ
ズの点で顕著な差が認められた。その結果を第3表に示
す。
As a result of measuring the physical properties of both films, significant differences in impact strength and haze were observed. The results are shown in Table 3.

実施例7〜8 実施例6において、REVOHの種類を変えて、その他は同
操作により厚さ60μのフイルムを得た。これらの物性を
実施例6と同様に測定した。結果を第4表に示す。
Examples 7 to 8 In Example 6, the type of REVOH was changed, and the other operations were the same, to obtain a film having a thickness of 60 μm. These physical properties were measured as in Example 6. The results are shown in Table 4.

G.作用効果 本発明によるREVOHまたはREVOHとEVOHの混合物と、オレ
フイン系樹脂との組成物を用いたフイルム、シート、容
器等は、従来のEVOHとオレフイン系樹脂との組成物によ
るものより格段に優れた機械的性能、透明性を有し、各
種包装材料分野に広く好適に用いられる。
G. Action and effect REVOH or a mixture of REVOH and EVOH according to the present invention, a film, a sheet, a container, etc. using a composition of an olefin resin are significantly more than those of a conventional composition of EVOH and an olefin resin. It has excellent mechanical performance and transparency, and is widely and suitably used in various packaging material fields.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】末端にRS基(但しRは炭素数4〜30の炭化
水素、Sは硫黄原子)を有するエチレン−ビニルアルコ
ール系共重合体または該共重合体と末端にRS基を有さな
いエチレン−ビニルアルコール系共重合体の混合物
(A)およびオレフィン系樹脂(B)からなり、かつ
(A)と(B)の重量比が95:5ないし5:95である樹脂組
成物。
1. An ethylene-vinyl alcohol-based copolymer having an RS group at the terminal (wherein R is a hydrocarbon having 4 to 30 carbon atoms, S is a sulfur atom), or an RS group at the terminal with the copolymer. A resin composition comprising an ethylene-vinyl alcohol copolymer mixture (A) and an olefin resin (B), and the weight ratio of (A) to (B) is 95: 5 to 5:95.
【請求項2】(A)が、末端にRS基を有するエチレン−
ビニルアルコール系共重合体と、末端にRS基を有さない
エチレン−ビニルアルコール系共重合体の混合物であ
り、その重量比が95:5ないし5:95である特許請求の範囲
第1項記載の樹脂組成物。
2. (A) is an ethylene-containing terminal RS group
The mixture of a vinyl alcohol copolymer and an ethylene-vinyl alcohol copolymer having no RS group at the terminal, the weight ratio of which is 95: 5 to 5:95. Resin composition.
JP3528487A 1987-02-17 1987-02-17 Resin composition Expired - Fee Related JPH0788452B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3528487A JPH0788452B2 (en) 1987-02-17 1987-02-17 Resin composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3528487A JPH0788452B2 (en) 1987-02-17 1987-02-17 Resin composition

Publications (2)

Publication Number Publication Date
JPS63202638A JPS63202638A (en) 1988-08-22
JPH0788452B2 true JPH0788452B2 (en) 1995-09-27

Family

ID=12437474

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3528487A Expired - Fee Related JPH0788452B2 (en) 1987-02-17 1987-02-17 Resin composition

Country Status (1)

Country Link
JP (1) JPH0788452B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5349023A (en) * 1991-12-12 1994-09-20 Kuraray Co., Ltd. Vinyl alcohol copolymer having terminal amino group

Also Published As

Publication number Publication date
JPS63202638A (en) 1988-08-22

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