JP3430551B2 - Olefin resin molded product with gas barrier properties - Google Patents

Olefin resin molded product with gas barrier properties

Info

Publication number
JP3430551B2
JP3430551B2 JP10100293A JP10100293A JP3430551B2 JP 3430551 B2 JP3430551 B2 JP 3430551B2 JP 10100293 A JP10100293 A JP 10100293A JP 10100293 A JP10100293 A JP 10100293A JP 3430551 B2 JP3430551 B2 JP 3430551B2
Authority
JP
Japan
Prior art keywords
gas barrier
film
molded product
modified
resin molded
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
JP10100293A
Other languages
Japanese (ja)
Other versions
JPH06306198A (en
Inventor
智美 中野
正之 江上
正文 服部
明 水野
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.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Chemical Corp
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 Mitsubishi Chemical Corp filed Critical Mitsubishi Chemical Corp
Priority to JP10100293A priority Critical patent/JP3430551B2/en
Priority to EP19940106233 priority patent/EP0622399B1/en
Priority to DE1994625296 priority patent/DE69425296T2/en
Publication of JPH06306198A publication Critical patent/JPH06306198A/en
Priority to US08/583,859 priority patent/US5763088A/en
Application granted granted Critical
Publication of JP3430551B2 publication Critical patent/JP3430551B2/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】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、食品、電子部品等を保
護する為に用いられるガスバリアー性の優れたオレフィ
ン系樹脂成形品に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an olefin resin molded article having excellent gas barrier properties, which is used for protecting foods, electronic parts and the like.

【0002】[0002]

【従来の技術】食品、電子工業部品等をフィルム、容器
で包装し、酸素の透過を抑制することにより内容物の酸
化を防止し、品質を長期間保つことが提案されている。
例えば、特公昭53−12953号公報には、厚さが5
〜300μmのポリエチレンテレフタレート、セロファ
ン、ナイロン、ポリプロピレン、ポリエチレン等のフレ
キシブルなプラスチックフィルムの少なくとも片面に、
一般式Six y (x=1または2、y=0,1,2ま
たは3)なる組成の珪素酸化物の厚さ100〜3000
オングストロームの透明薄膜層を設けた高度の耐透気性
と耐透湿性を有する透明フレキシブルプラスチックフィ
ルムが開示されている。
2. Description of the Related Art It has been proposed to wrap foods, electronic parts, etc. in a film or a container to prevent the permeation of oxygen to prevent the contents from being oxidized and to maintain the quality for a long time.
For example, in Japanese Patent Publication No. 53-12953, the thickness is 5
-300 μm polyethylene terephthalate, cellophane, nylon, polypropylene, polyethylene or other flexible plastic film on at least one side,
Thickness of silicon oxide having a composition represented by the general formula: Si x O y (x = 1 or 2, y = 0, 1, 2, or 3) 100 to 3000
A transparent flexible plastic film having a high degree of air permeability and moisture resistance provided with an angstrom transparent thin film layer is disclosed.

【0003】また、特開昭63−237940号公報に
は、上記フレキシブルプラスチックフィルムの少なくと
も一方の面に、In、Sn、Zn、ZrおよびTiから
なる群から選ばれた一種の金属の金属酸化物がスパッタ
リングにより形成され、更にこの上に透明なヒートシー
ル性樹脂膜がコートされた透明ガスバリアーフィルムが
開示されている。
Further, Japanese Patent Laid-Open No. 63-237940 discloses a metal oxide of one kind of metal selected from the group consisting of In, Sn, Zn, Zr and Ti on at least one surface of the flexible plastic film. Is disclosed by sputtering, and a transparent heat-sealable resin film is coated on the transparent gas barrier film.

【0004】フィルム素材がポリエチレンテレフタレー
ト、ナイロン、セロファンのような極性基を有する樹脂
であるときは、フィルムと無機酸化膜との密着力が十分
で、ガスバリアー性も良好である。しかし、ポリプロピ
レン、ポリエチレンのような極性基を有しないポリオレ
フィンの成形品の表面に、上記のような無機酸化物から
なる蒸着薄膜を形成させても、ポリオレフィン成形品と
薄膜との密着力が弱いので、この蒸着物にヒートシール
性を付与するために成形品を構成するポリオレフィンの
融点よりも低い融点を有するヒートシール性樹脂をラミ
ネートする場合や、このラミネート物を用い、製袋や蓋
シールの二次加工を行う際や、これら袋を用いたり、容
器内に収容物を充填し、更にはレトルト殺菌する際に外
部応力や熱が成形品に加わって無機酸化薄膜がポリオレ
フィン成形品より剥離し、ガスバリアー性が低下し、実
用に耐えない問題がある。
When the film material is a resin having a polar group such as polyethylene terephthalate, nylon or cellophane, the film and the inorganic oxide film have sufficient adhesion and a good gas barrier property. However, even if a vapor-deposited thin film made of the above inorganic oxide is formed on the surface of a polyolefin molded product having no polar groups such as polypropylene and polyethylene, the adhesion between the polyolefin molded product and the thin film is weak. When laminating a heat-sealable resin having a melting point lower than that of the polyolefin constituting the molded article in order to impart heat-sealing property to the vapor-deposited product, or by using this laminated product, it can be used for bag making or lid sealing. When performing the next processing, using these bags, filling the contents in the container, further when external sterilization and heat are applied to the molded product during retort sterilization, the inorganic oxide thin film peels from the polyolefin molded product, There is a problem that the gas barrier property is lowered and it cannot be put to practical use.

【0005】[0005]

【発明が解決しようとする課題】本発明は、無機酸化薄
膜が蒸着されたオレフィン系樹脂成形品であっても、こ
れの二次加工時や使用時に無機酸化薄膜が剥離せず、ガ
スバリアー性が低下しない樹脂成形品を提供することを
目的とするものである。
DISCLOSURE OF THE INVENTION The present invention has a gas barrier property even when an olefin resin molded article having an inorganic oxide thin film deposited thereon is not peeled off during secondary processing or during use. It is an object of the present invention to provide a resin molded product that does not deteriorate.

【0006】[0006]

【課題を解決する手段】本発明は、α,β−エチレン性
不飽和カルボン酸でグラフト変性した変性ポリプロピレ
ンであって、該変性ポリプロピレン中のα,β−エチレ
ン性不飽和カルボン酸に基づく構成単位濃度が0.01
〜10重量%である変性ポリプロピレンの成形品の表面
に、無機酸化物薄膜を蒸着により形成した、ガスバリア
ー性の付与されたオレフィン系樹脂成形品を提供するも
のである。
The present invention is a modified polypropylene graft-modified with an α, β-ethylenically unsaturated carboxylic acid, wherein the structural unit based on the α, β-ethylenically unsaturated carboxylic acid in the modified polypropylene. The concentration is 0.01
Provided is an olefin-based resin molded product having a gas barrier property, which is formed by depositing an inorganic oxide thin film on the surface of a modified polypropylene molded product of 10% by weight.

【0007】[0007]

【作用】本発明では、基材の変性ポリオレフィンとし
て、特定量のカルボキシル基(−COOH)を有する変
性ポリプロピレンを用いたことで、無機酸化物蒸着膜と
の密着性が強固となる。
In the present invention, as the modified polyolefin of the substrate, the modified polypropylene having a specific amount of carboxyl group (-COOH) is used, so that the adhesion to the inorganic oxide vapor deposition film becomes strong.

【0008】[0008]

【発明の具体的な説明】変性ポリオレフィン 本発明では、基材の変性ポリオレフィンは、α,β−エ
チレン性不飽和カルボン酸(その無水物も含む)をポリ
プロピレンにグラフト重合させることにより得られる。
グラフト重合させる手法としては、ポリプロピレン、
α,β−エチレン性不飽和カルボン酸及び触媒を押出機
中で溶融混練する方法(特公昭43−27421号、特
公昭59−15127号)、または適当な溶媒中に溶解
しているポリプロピレンにグラフト用のα,β−エチレ
ン性不飽和カルボン酸及び触媒を添加して加熱攪拌する
方法(特公昭44−15422号、特公昭52−305
46)等がある。
DETAILED DESCRIPTION OF THE INVENTION Modified Polyolefin In the present invention, the modified polyolefin of the substrate is obtained by graft-polymerizing α, β-ethylenically unsaturated carboxylic acid (including its anhydride) on polypropylene.
As the method of graft polymerization, polypropylene,
A method of melt-kneading an α, β-ethylenically unsaturated carboxylic acid and a catalyst in an extruder (Japanese Examined Patent Publication No. 43-27421, Japanese Examined Patent Publication No. 59-15127) or grafting on polypropylene dissolved in a suitable solvent. A method for adding α, β-ethylenically unsaturated carboxylic acid and a catalyst for heating and stirring (Japanese Patent Publication No. 44-15422 and Japanese Patent Publication No. 52-305).
46) etc.

【0009】変性させるポリプロピレンとしては、プロ
ピレンの単独重合体の他に、プロピレンとエチレンその
他のα−オレフィンとの共重合体、例えばエチレン−プ
ロピレン共重合体、プロピレン−ブテン−1、プロピレ
ン−エチレン−ブテン−1共重合体等のα−オレフィン
同士の結晶性重合体も含む。これらの重合体、共重合体
をブレンドして使用しても良い。また、変性したポリオ
レフィンを未変性のポリオレフィンで希釈して用いても
良い。変性ポリプロピレン、もしくは未変性ポリオレフ
ィンで希釈された変性ポリプロピレンのMFR(JIS
K−7210)は、成形品が得られれば良く、通常
0.1〜100g/10分、好ましくは0.5〜20g
/10分である。
As the polypropylene to be modified, in addition to a propylene homopolymer, a copolymer of propylene and ethylene or other α-olefin, for example, an ethylene-propylene copolymer, propylene-butene-1, propylene-ethylene- Also included are crystalline polymers of α-olefins such as butene-1 copolymer. You may blend and use these polymers and copolymers. Further, the modified polyolefin may be diluted with an unmodified polyolefin before use. MFR of modified polypropylene or modified polypropylene diluted with unmodified polyolefin (JIS
K-7210) has only to be a molded product, and is usually 0.1 to 100 g / 10 minutes, preferably 0.5 to 20 g.
/ 10 minutes.

【0010】また、成形品のα,β−エチレン性不飽和
カルボン酸に基づく構成単位濃度が上記範囲より少ない
と、無機酸化物薄膜との結合力が十分でなく、また上記
範囲より多くしても結合力の向上が見られず、さらにグ
ラフト反応時に分解反応が起こるため、低分子量分が増
加し結合力が低下するなどの問題が発生する。
Further, if the concentration of the constituent unit based on α, β-ethylenically unsaturated carboxylic acid in the molded product is less than the above range, the binding force with the inorganic oxide thin film is insufficient, and if it is more than the above range. However, there is no improvement in the binding force, and since a decomposition reaction occurs during the grafting reaction, there arises a problem that the low molecular weight component increases and the binding force decreases.

【0011】一方、ポリプロピレンにグラフトさせる
α,β−エチレン性不飽和カルボン酸としては、アクリ
ル酸、マレイン酸、フマル酸、イタコン酸、ハイミック
酸またはそれらの無水物等が挙げられるが、中でもアク
リル酸、無水マレイン酸、特に無水マレイン酸が望まし
い。
On the other hand, examples of the α, β-ethylenically unsaturated carboxylic acid to be grafted on polypropylene include acrylic acid, maleic acid, fumaric acid, itaconic acid, hymic acid and their anhydrides. Among them, acrylic acid is preferable. , Maleic anhydride, especially maleic anhydride is preferred.

【0012】成形品 成形品は押出成形、射出成形、真空成形、中空成形等に
よりフィルム、シート、容器、箱等に成形される。又、
変性ポリオレフィンとポリエチレン、ポリプロピレン、
エチレン・酢酸ビニル共重合体、ポリアミド、ポリブチ
レンテレフタレート、ポリエチレンテレフタレート、ポ
リフェニレンスルフィド、ポリフェニレンエーテル、ポ
リカーボネート等の熱可塑性樹脂との積層体構造として
も良い。また、フィルム、シートは延伸されたものが好
ましい。
Molded Article The molded article is formed into a film, sheet, container, box or the like by extrusion molding, injection molding, vacuum molding, blow molding or the like. or,
Modified polyolefin and polyethylene, polypropylene,
It may have a laminate structure with a thermoplastic resin such as an ethylene / vinyl acetate copolymer, polyamide, polybutylene terephthalate, polyethylene terephthalate, polyphenylene sulfide, polyphenylene ether, or polycarbonate. The film or sheet is preferably stretched.

【0013】肉厚はフィルムにおいて5〜200μm、
シートにおいて200〜1,500μm、小型容器、箱
型等のハウジングにおいて300〜2,500μm、タ
ンク容器、20リットルの薬品容器において1〜10m
mが一般である。成形品は必要によりその変性ポリオレ
フィンの表面をコロナ放電処理、オゾン処理、グロー放
電処理、プラズマ処理、化学薬品による酸化処理を施し
ても良い。しかし、一般に無機酸化物の薄膜の蒸着がこ
れら酸化処理を伴って行われることが多いので、成形
中、あるいは成形後にわざわざかかる酸化処理をする必
要はない。
The thickness of the film is 5 to 200 μm,
200 to 1,500 μm for sheets, 300 to 2,500 μm for small containers, box-shaped housings, etc., 1 to 10 m for tank containers and 20 liter chemical containers.
m is common. If necessary, the molded product may be subjected to corona discharge treatment, ozone treatment, glow discharge treatment, plasma treatment, or oxidation treatment with a chemical agent on the surface of the modified polyolefin. However, in general, a thin film of an inorganic oxide is often vapor-deposited together with these oxidation treatments, and thus it is not necessary to perform the oxidation treatment during or after the molding.

【0014】無機酸化物の蒸着 無機酸化物の薄膜としては、SiOx 、SnOx 、Zn
x 、IrOx 等の通常200〜4,000オングスト
ローム、好ましくは300〜3,000オングストロー
ムのものが利用される。この蒸着膜の厚みは、透明性、
蒸着速度、ガスバリアー性、フィルムの巻き取り性等か
ら制約される。蒸着法としては、高周波誘導加熱方式の
蒸着機内で成形品を真空下(1×10-3〜1×106
ール)で無機酸化物を蒸着する方法(特公昭53−12
963号);予め排気し、真空化した蒸着機内で揮発し
た有機シリコン化合物、酸素及び不活性ガスを含むガス
流をマグネトロングロー放電によってプラズマを発生さ
せてSiOx を該蒸着機内で成形品に蒸着させる方法
(特開昭64−87772号、USP4、557、94
6号、USP4、599、678号)等がある。又、1
990年11月発刊の工業材料、第38巻、第14号の
第104〜105頁で、イオンプレーティング法、高周
波プラズマCVD法、電子ビーム(EB)蒸着法、スパ
ッタリング法として分類され、その原理が紹介されてい
る。
Vapor Deposition of Inorganic Oxide As a thin film of inorganic oxide, SiO x , SnO x , Zn
O x, usually 200 to 4,000 Å, such as IrO x, it is preferably utilized as a 300 to 3,000 angstroms. The thickness of this deposited film is
It is restricted by vapor deposition rate, gas barrier property, film winding property, and the like. As the vapor deposition method, a method of depositing an inorganic oxide on a molded article under vacuum (1 × 10 −3 to 1 × 10 6 torr) in a high frequency induction heating type vapor deposition machine (Japanese Patent Publication No. 53-12).
963); a gas flow containing an organosilicon compound, oxygen, and an inert gas which has been evacuated and evacuated in advance in a vapor deposition machine is used to generate plasma by magnetron glow discharge to deposit SiO x on a molded article in the vapor deposition machine. Method (JP-A-64-87772, USP 4,557,94)
No. 6, USP 4,599,678) and the like. Again 1
Industrial materials published in November 990, Volume 38, No. 14, pp. 104 to 105, are classified as ion plating method, high frequency plasma CVD method, electron beam (EB) vapor deposition method, and sputtering method, and the principle thereof. Has been introduced.

【0015】[0015]

【実施例】以下、実施例により、本発明を詳細に説明す
るが、これにより本発明の範囲は特に限定されるもので
はない。
The present invention will be described in detail below with reference to examples, but the scope of the present invention is not particularly limited thereby.

【0016】変性ポリプロピレンの製造例 例1 ポリプロピレン(MFR 2g/10分、密度 0.9
05g/cm3 )のパウダー100重量部に、過酸化ベ
ンゾイル0.8重量部、無水マレイン酸1.2重量部を
添加後、ヘンシェルミキサーにて混合し、押出機にてダ
イより220℃でストランド状に押出し、水冷後、カッ
ティングしてペレットを得た。この変性ポリプロピレン
のペレットを沸騰したキシレンに溶解して大量のアセト
ンにて再沈させた後、赤外吸収スペクトル分析法で変性
ポリプロピレン中に占める無水マレイン酸に基づく構成
単位濃度を測定したところ、0.7重量%がグラフト共
重合していた。
Production Example of Modified Polypropylene Example 1 Polypropylene (MFR 2 g / 10 min, density 0.9
(05 g / cm 3 ) powder (100 parts by weight), benzoyl peroxide (0.8 parts by weight) and maleic anhydride (1.2 parts by weight) were added, and the mixture was mixed with a Henschel mixer. The mixture was extruded into a shape, cooled with water, and then cut to obtain pellets. The modified polypropylene pellets were dissolved in boiling xylene, reprecipitated with a large amount of acetone, and the concentration of the structural unit based on maleic anhydride in the modified polypropylene was measured by infrared absorption spectroscopy. Graft copolymerization was carried out in an amount of 0.7% by weight.

【0017】例2 エチレン−プロピレン共重合体(エチレン含有5%、M
FR 1g/10分、密度 0.89g/cm3 )のパ
ウダーを100重量部に過酸化ベンゾイル0.8重量
部、無水マレイン酸1.2重量部を添加し、例1と同様
に変性共重合体を製造した。変性共重合体に占める無水
マレイン酸成分濃度を測定したところ0.9重量%であ
った。
Example 2 Ethylene-propylene copolymer (ethylene content 5%, M
FR 1 g / 10 min, density 0.89 g / cm 3 ) 100 parts by weight of powder to which 0.8 parts by weight of benzoyl peroxide and 1.2 parts by weight of maleic anhydride were added, and modified copolyester as in Example 1 A coalesce was manufactured. The concentration of the maleic anhydride component in the modified copolymer was measured and found to be 0.9% by weight.

【0018】変性ポリエチレンの製造例 例3 直鎖状低密度ポリエチレン(MFR 2g/10分、密
度 0.920g/cm3 、エチレン含有が91.0重
量%、ヘキセン含有が9.0重量%)100重量部に
2,5−ジメル−2,5−ジ(t−ブチルパ−オキシ)
ヘキサン0.04重量部および無水マレイン酸2重量部
を添加後、ヘンシェルミキサーにて混合し、押出機にて
ダイより180℃でストランド状に押出し、水冷後、カ
ッティングしてペレットを得た。この変性ポリプロピレ
ンのペレットを沸騰したキシレンに溶解して大量のアセ
トンにて再沈させた後、赤外吸収スペクトル分析法で変
性ポリエチレン中に占める無水マレイン酸に基づく構成
単位濃度を測定したところ、1.9重量%がグラフト共
重合していた。
Production Example of Modified Polyethylene Example 3 Linear low-density polyethylene (MFR 2 g / 10 min, density 0.920 g / cm 3 , ethylene content 91.0% by weight, hexene content 9.0% by weight) 100 2,5-dimel-2,5-di (t-butylperoxy) in parts by weight
Hexane (0.04 parts by weight) and maleic anhydride (2 parts by weight) were added, mixed with a Henschel mixer, extruded into a strand at 180 ° C. from a die with an extruder, cooled with water, and cut to obtain pellets. The modified polypropylene pellets were dissolved in boiling xylene, reprecipitated with a large amount of acetone, and the concentration of the constituent unit based on maleic anhydride in the modified polyethylene was measured by infrared absorption spectroscopy. Graft copolymerization was performed in an amount of 0.9% by weight.

【0019】実施例1 例1で得た変性ポリプロピレンを押出機で溶融し、T−
ダイより238℃でシート状に押し出し、金属ロールで
冷却して厚さ1mmのシートを得た。このシートを12
0℃に加熱し、ロール群の周速差を利用して縦方向に5
倍延伸した。ついで、テンターオーブン内に導き、15
7℃に再加熱した後、テンターを用いて横方向に10倍
延伸し、163℃でアニーリング処理し、コロナ放電処
理して肉厚が20μmの二軸延伸フィルムを得た。
Example 1 The modified polypropylene obtained in Example 1 was melted in an extruder to obtain T-
A sheet having a thickness of 1 mm was obtained by extruding a sheet at 238 ° C. from a die and cooling with a metal roll. This sheet 12
Heat to 0 ° C, and use the difference in peripheral speed of the rolls to move vertically 5
It was stretched twice. Then, lead it into the tenter oven, 15
After reheating to 7 ° C., it was stretched 10 times in the transverse direction using a tenter, annealed at 163 ° C., and corona discharge treated to obtain a biaxially stretched film having a thickness of 20 μm.

【0020】このコロナ放電処理された二軸延伸フィル
ムを、プラズマ蒸着装置内に置き、装置内を1×10-6
トールの減圧下にしたのち、ヘキサメチルジシロキサン
3容量部、酸素3容量部、ヘリウム20容量部、アルゴ
ン13容量部の混合気体を導き、不平衡型マグネトロン
よりグロー放電を行ってプラズマを発生させSiO2
薄膜を二軸延伸フィルム状に蒸着させた。蒸着時のグロ
ー放電の条件は、得られたSiO2 蒸着二軸延伸フィル
ムの酸素透過率が5.0cc/m2 ・atm・day
(JIS 1707−35)となるように設定した。
This biaxially stretched film subjected to corona discharge treatment was placed in a plasma deposition apparatus, and the inside of the apparatus was set at 1 × 10 -6.
After reducing the pressure under a reduced pressure of torr, a mixed gas of 3 parts by volume of hexamethyldisiloxane, 3 parts by volume of oxygen, 20 parts by volume of helium, and 13 parts by volume of argon was introduced, and glow discharge was performed from the unbalanced magnetron to generate plasma. A thin film of SiO 2 was deposited in the form of a biaxially stretched film. The glow discharge conditions during vapor deposition were such that the obtained SiO 2 vapor-deposited biaxially stretched film had an oxygen permeability of 5.0 cc / m 2 · atm · day.
(JIS 1707-35).

【0021】実施例2 例1で得た変性ポリプロピレン5重量部を、未変性ポリ
プロピレン(MFR0.8g/10分、密度 0.95
0g/cm3 )95重量部で希釈したもの(希釈物中の
マレイン酸の構成単位濃度 0.035重量%)を変性
ポリプロピレンの代わりに用いる他は実施例1と同様に
してSiO2 蒸着二軸延伸ポリプロピレンフィルムを製
造した。
Example 2 5 parts by weight of the modified polypropylene obtained in Example 1 was added to unmodified polypropylene (MFR 0.8 g / 10 min, density 0.95).
0 g / cm 3 ) diluted with 95 parts by weight (concentration of maleic acid constituent in the diluted product: 0.035% by weight) is used instead of the modified polypropylene in the same manner as in Example 1 for biaxial deposition of SiO 2. A stretched polypropylene film was produced.

【0022】実施例3 例2で得た変性共重合体と実施例2で使用した未変性ポ
リプロピレンを、別々の押出機で溶融したものを一台の
ダイに供給し、ダイ内で層状に重ね、押し出して変性共
重合体の層の厚さが0.1mm、未変性ポリプロピレン
層の厚さが0.9mm、合計厚さが1mmのシートを作
成し実施例1と同様にして延伸し厚さ20μmのフィル
ムを作成し、変性共重合体側をコロナ放電処理後、実施
例1と同様にしてSiO2 蒸着二軸延伸フィルムを製造
した。
Example 3 The modified copolymer obtained in Example 2 and the unmodified polypropylene used in Example 2 were melted by different extruders and fed to one die, which was layered in the die. Then, a sheet having a thickness of the modified copolymer layer of 0.1 mm, an unmodified polypropylene layer of 0.9 mm, and a total thickness of 1 mm was extruded to form a sheet and stretched in the same manner as in Example 1. A 20 μm film was prepared, the modified copolymer side was subjected to corona discharge treatment, and then a SiO 2 vapor-deposited biaxially stretched film was produced in the same manner as in Example 1.

【0023】比較例1 未変性ポリプロピレン(MFR 0.8g/10分、密
度 0.905g/cm3 )を変性ポリプロピレンの代
わりに用いる他は実施例1と同様にしてSiO2 蒸着二
軸延伸ポリプロピレンフィルムを製造した。
Comparative Example 1 A SiO 2 vapor-deposited biaxially oriented polypropylene film was prepared in the same manner as in Example 1 except that unmodified polypropylene (MFR 0.8 g / 10 min, density 0.905 g / cm 3 ) was used instead of the modified polypropylene. Was manufactured.

【0024】比較例2 例1で得た変性ポリプロピレン1重量部を、未変性ポリ
プロピレン(MFR0.8g/10分、密度 0.90
5g/cm3 )99重量部で希釈したもの(マレイン酸
の構成単位濃度 0.007重量%)を変性ポリプロピ
レンの代わりに用いる他は実施例1と同様にしてSiO
2 蒸着二軸延伸ポリプロピレンフィルムを製造した。
Comparative Example 2 1 part by weight of the modified polypropylene obtained in Example 1 was added to unmodified polypropylene (MFR 0.8 g / 10 min, density 0.90).
5 g / cm 3 ) 99 parts by weight (maleic acid constituent unit concentration 0.007% by weight) diluted with SiO 2 in the same manner as in Example 1 except that the modified polypropylene was used.
Two vapor-deposited biaxially oriented polypropylene films were produced.

【0025】比較例3 例3で得た変性ポリエチレンを、押出機で溶融し、イン
フレダイより160℃で筒状に押し出し、バブルの内部
に空気を吹き込んでブロー比2まで膨張させた後、コロ
ナ放電処理を行い、肉厚が40μmの変性ポリエチレン
フィルムを得た。このフィルムを用いて実施例1と同様
にSiO2 蒸着ポリエチレンフィルムを製造した。
Comparative Example 3 The modified polyethylene obtained in Example 3 was melted by an extruder and extruded into a cylindrical shape at 160 ° C. from an inflation die, and air was blown into the bubble to expand it to a blow ratio of 2 and then the corona. Electric discharge treatment was performed to obtain a modified polyethylene film having a thickness of 40 μm. Using this film, a SiO 2 vapor-deposited polyethylene film was produced in the same manner as in Example 1.

【0026】比較例4 未変性直鎖状低密度ポリエチレン(MFR 2g/10
分、密度 0.920g/cm3 )を変性ポリエチレン
の代わりに用いる他は、比較例3と同様にしてSiO2
蒸着ポリエチレンフィルムを製造した。なお、全ての延
伸フィルムの酸素透過率が5.0cc/m2 ・atm・
dayとなるようにグロー放電の条件を変えて行った。
Comparative Example 4 Unmodified linear low density polyethylene (MFR 2 g / 10
Min, except for using a density 0.920 g / cm 3) in place of the modified polyethylene is in the same manner as in Comparative Example 3 SiO 2
A vapor-deposited polyethylene film was produced. The oxygen permeability of all stretched films was 5.0 cc / m 2 · atm ·
The glow discharge conditions were changed so as to obtain the day.

【0027】評価 (1)外応力に対する変化 実施例1〜3、および比較例1〜4で得たSiO2 蒸着
フィルムを、各立計器(株)製ゲルボテスターを用い、
フィルムを筒状に丸めたのち、この筒の両端をテスター
の把持器具に固定し、10回、±90度回転ねじりの繰
り返しを行った後、酸素透過率を測定した。その測定値
を表1に示す。 (2)二次加工に対する変化 実施例1〜3、および比較例1〜4で得たSiO2 蒸着
フィルムのSiO2 蒸着面に、ラミネータ装置を用い、
メルトインデックス5g/10分、密度0.922g/
cm3 の低密度ポリエチレンを320℃で20μmの肉
厚のフィルム状にT−ダイより押し出し、ラミネートし
た。このラミネート物の酸素透過率を表1に示す。
Evaluation (1) Change with respect to external stress The SiO 2 vapor-deposited films obtained in Examples 1 to 3 and Comparative Examples 1 to 4 were used in a gel votester manufactured by Rikiki Co., Ltd.
After rolling the film into a tube shape, both ends of the tube were fixed to a gripping device of a tester, and a twist of ± 90 ° was repeated 10 times, and then the oxygen transmission rate was measured. The measured values are shown in Table 1. (2) the SiO 2 deposition surface of the SiO 2 deposited film obtained by the change Examples 1-3, and Comparative Examples 1 to 4 for the secondary processing, using a laminator apparatus,
Melt index 5g / 10min, density 0.922g /
cm 3 of low density polyethylene was extruded from a T-die at 320 ° C. into a film having a thickness of 20 μm and laminated. The oxygen transmission rate of this laminate is shown in Table 1.

【0028】[0028]

【表1】単位:cc/m2 ・atm・day [Table 1] Unit: cc / m 2 · atm · day

【0029】[0029]

【発明の効果】本発明の無機酸化物が蒸着したオレフィ
ン系樹脂成形品は、二次加工時や使用時に、熱や力が加
わってもガスバリアー性が低下しない樹脂成形品であ
る。従って、レトルトパウチ包装材、IC包装材として
も有用である。
EFFECT OF THE INVENTION The olefin resin molded article on which the inorganic oxide of the present invention is vapor deposited is a resin molded article whose gas barrier property does not deteriorate even when heat or force is applied during secondary processing or during use. Therefore, it is also useful as a retort pouch packaging material and an IC packaging material.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 水野 明 三重県四日市市東邦町1番地 三菱油化 株式会社四日市総合研究所内 (56)参考文献 特開 昭58−110242(JP,A) 特開 平3−244535(JP,A) 特開 平5−131590(JP,A) 特開 平6−190961(JP,A) 特開 平5−287103(JP,A) 特開 平6−298263(JP,A) 特開 昭55−155035(JP,A) 特開 昭60−137940(JP,A) 特開 平5−51420(JP,A) 特開 平4−7139(JP,A) (58)調査した分野(Int.Cl.7,DB名) C08J 7/04 - 7/06 C08L 23/00 - 23/36 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Akira Mizuno 1 Toho-cho, Yokkaichi-shi, Mie Mitsubishi Yuka Co., Ltd. inside the Yokkaichi Research Institute (56) Reference JP-A-58-110242 (JP, A) JP-A 3-244535 (JP, A) JP 5-131590 (JP, A) JP 6-190961 (JP, A) JP 5-287103 (JP, A) JP 6-298263 (JP, A) JP 55-155035 (JP, A) JP 60-137940 (JP, A) JP 5-51420 (JP, A) JP 4-7139 (JP, A) (58) Survey Areas (Int.Cl. 7 , DB name) C08J 7 /04-7/06 C08L 23/00-23/36

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 α,β−エチレン性不飽和カルボン酸で
グラフト変性した変性ポリプロピレンであって、該変性
ポリプロピレン中のα,β−エチレン性不飽和カルボン
酸に基づく構成単位濃度が0.01〜10重量%である
変性ポリプロピレンの成形品の表面に、無機酸化物薄膜
蒸着により形成した、ガスバリアー性の付与されたオ
レフィン系樹脂成形品。
1. A modified polypropylene graft-modified with an α, β-ethylenically unsaturated carboxylic acid, wherein the concentration of the constituent unit based on the α, β-ethylenically unsaturated carboxylic acid in the modified polypropylene is 0.01 to. An olefin resin molded product having a gas barrier property, which is formed by depositing an inorganic oxide thin film on the surface of a modified polypropylene molded product of 10% by weight.
【請求項2】 α,β−エチレン性不飽和カルボン酸が
無水マレイン酸である、請求項1のガスバリアー性の付
与されたオレフィン系樹脂成形品。
2. The olefin resin molded article having gas barrier properties according to claim 1, wherein the α, β-ethylenically unsaturated carboxylic acid is maleic anhydride.
【請求項3】 無機酸化物薄膜の厚みが200〜4,0
00オングストロームである、請求項1又は2のガスバ
リアー性の付与されたオレフィン系樹脂成形品。
3. The inorganic oxide thin film has a thickness of 200 to 4,0.
The olefin-based resin molded article having a gas barrier property according to claim 1 or 2, which is 00 angstrom.
【請求項4】 無機酸化物薄膜がSiOxからなる請求
項1〜3のいずれかのガスバリヤー性の付与されたオレ
フィン系樹脂組成物。
4. The olefin resin composition having a gas barrier property according to claim 1, wherein the inorganic oxide thin film is made of SiOx.
【請求項5】 成型品が変性ポリプロピレンからなる延
伸シート又はフィルムであって、該シート又は該フィル
ムの表面に、無機酸化物薄膜を形成した、請求項1ない
し4のいずれかのガスバリヤー性の付与されたオレフィ
ン系樹脂成形品。
5. The gas barrier property according to claim 1, wherein the molded product is a stretched sheet or film made of modified polypropylene, and an inorganic oxide thin film is formed on the surface of the sheet or the film. The given olefin resin molded product.
JP10100293A 1993-04-27 1993-04-27 Olefin resin molded product with gas barrier properties Expired - Lifetime JP3430551B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP10100293A JP3430551B2 (en) 1993-04-27 1993-04-27 Olefin resin molded product with gas barrier properties
EP19940106233 EP0622399B1 (en) 1993-04-27 1994-04-21 Olefin resin-based articles having gas barrier properties
DE1994625296 DE69425296T2 (en) 1993-04-27 1994-04-21 Products based on olefin resins with properties for gas impermeability
US08/583,859 US5763088A (en) 1993-04-27 1996-01-11 Olefin resin-based articles having gas barrier properties

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10100293A JP3430551B2 (en) 1993-04-27 1993-04-27 Olefin resin molded product with gas barrier properties

Publications (2)

Publication Number Publication Date
JPH06306198A JPH06306198A (en) 1994-11-01
JP3430551B2 true JP3430551B2 (en) 2003-07-28

Family

ID=14289065

Family Applications (1)

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

Country Link
JP (1) JP3430551B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020067047A1 (en) 2018-09-28 2020-04-02 凸版印刷株式会社 Laminated film and packaging container

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6649235B2 (en) * 1998-08-17 2003-11-18 Hoechst Trespaphan Gmbh Process for producing coated polymeric articles and the articles produced thereby
JP2002179068A (en) * 2000-12-20 2002-06-26 Toppan Printing Co Ltd Vessel with barrier property
JP6940224B2 (en) * 2016-09-07 2021-09-22 リンテック株式会社 Gas barrier laminate and seal

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020067047A1 (en) 2018-09-28 2020-04-02 凸版印刷株式会社 Laminated film and packaging container

Also Published As

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