JPS6341550A - Resin composition for molding film - Google Patents
Resin composition for molding filmInfo
- Publication number
- JPS6341550A JPS6341550A JP18581186A JP18581186A JPS6341550A JP S6341550 A JPS6341550 A JP S6341550A JP 18581186 A JP18581186 A JP 18581186A JP 18581186 A JP18581186 A JP 18581186A JP S6341550 A JPS6341550 A JP S6341550A
- Authority
- JP
- Japan
- Prior art keywords
- film
- ethylene
- density polyethylene
- composition
- packaging
- 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.)
- Granted
Links
- 239000011342 resin composition Substances 0.000 title claims description 5
- 238000000465 moulding Methods 0.000 title claims description 3
- 239000000203 mixture Substances 0.000 claims abstract description 36
- 239000005038 ethylene vinyl acetate Substances 0.000 claims abstract description 13
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 claims abstract description 13
- 229920005989 resin Polymers 0.000 claims abstract description 11
- 239000011347 resin Substances 0.000 claims abstract description 11
- 229920001862 ultra low molecular weight polyethylene Polymers 0.000 claims abstract description 10
- 229920001684 low density polyethylene Polymers 0.000 claims abstract description 9
- 239000004702 low-density polyethylene Substances 0.000 claims abstract description 9
- 239000004743 Polypropylene Substances 0.000 claims abstract description 8
- -1 polypropylene Polymers 0.000 claims abstract description 8
- 229920001155 polypropylene Polymers 0.000 claims abstract description 7
- 238000002156 mixing Methods 0.000 claims abstract description 6
- 229920006244 ethylene-ethyl acrylate Polymers 0.000 claims abstract description 5
- 229920000642 polymer Polymers 0.000 claims abstract description 5
- 229920012753 Ethylene Ionomers Polymers 0.000 claims abstract description 3
- 229920006242 ethylene acrylic acid copolymer Polymers 0.000 claims abstract description 3
- 238000002844 melting Methods 0.000 claims abstract description 3
- 230000008018 melting Effects 0.000 claims abstract description 3
- 229920001748 polybutylene Polymers 0.000 claims abstract 2
- 238000004806 packaging method and process Methods 0.000 abstract description 27
- 229920001577 copolymer Polymers 0.000 abstract description 4
- 229920000098 polyolefin Polymers 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 15
- 238000012360 testing method Methods 0.000 description 11
- 229920006302 stretch film Polymers 0.000 description 10
- 238000011156 evaluation Methods 0.000 description 9
- 230000000052 comparative effect Effects 0.000 description 8
- 239000004744 fabric Substances 0.000 description 7
- 239000000047 product Substances 0.000 description 5
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 4
- 239000004927 clay Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000009998 heat setting Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000004711 α-olefin Substances 0.000 description 4
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 3
- 239000005977 Ethylene Substances 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 235000013305 food Nutrition 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 229920001083 polybutene Polymers 0.000 description 3
- 230000037303 wrinkles Effects 0.000 description 3
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000008094 contradictory effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229920001038 ethylene copolymer Polymers 0.000 description 2
- 229920000554 ionomer Polymers 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- OJOWICOBYCXEKR-KRXBUXKQSA-N (5e)-5-ethylidenebicyclo[2.2.1]hept-2-ene Chemical compound C1C2C(=C/C)/CC1C=C2 OJOWICOBYCXEKR-KRXBUXKQSA-N 0.000 description 1
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 1
- 241000251468 Actinopterygii Species 0.000 description 1
- 206010008631 Cholera Diseases 0.000 description 1
- 241001149724 Cololabis adocetus Species 0.000 description 1
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical compound CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- 229920012485 Plasticized Polyvinyl chloride Polymers 0.000 description 1
- 101100023124 Schizosaccharomyces pombe (strain 972 / ATCC 24843) mfr2 gene Proteins 0.000 description 1
- 241000545760 Unio Species 0.000 description 1
- 229920006243 acrylic copolymer Polymers 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 210000000078 claw Anatomy 0.000 description 1
- 239000013065 commercial product Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 229940105990 diglycerin Drugs 0.000 description 1
- GPLRAVKSCUXZTP-UHFFFAOYSA-N diglycerol Chemical compound OCC(O)COCC(O)CO GPLRAVKSCUXZTP-UHFFFAOYSA-N 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 229920005648 ethylene methacrylic acid copolymer Polymers 0.000 description 1
- 239000005042 ethylene-ethyl acrylate Substances 0.000 description 1
- 229920006248 expandable polystyrene Polymers 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 229920005669 high impact polystyrene Polymers 0.000 description 1
- 239000004797 high-impact polystyrene Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 210000003127 knee Anatomy 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 235000010446 mineral oil Nutrition 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 239000004798 oriented polystyrene Substances 0.000 description 1
- PNJWIWWMYCMZRO-UHFFFAOYSA-N pent‐4‐en‐2‐one Natural products CC(=O)CC=C PNJWIWWMYCMZRO-UHFFFAOYSA-N 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000007127 saponification reaction Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 238000009864 tensile test Methods 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Landscapes
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、優れた押出成形性と延伸性を持つとともに1
ヒートシール性、衝撃強度特性、引張強度特性、柔軟性
、耐寒性、透明性等の数多くの優れた特性を有するポリ
オレフィン系フィルムを得ることのできる組成物に関す
る。[Detailed description of the invention] [Industrial application field] The present invention has excellent extrusion moldability and stretchability, and
The present invention relates to a composition capable of producing a polyolefin film having many excellent properties such as heat sealability, impact strength properties, tensile strength properties, flexibility, cold resistance, and transparency.
この組成物は複合フィルムの主体となる樹脂層を構成す
るものとして有用なものであり、このような複合フィル
ムは食品包装用ストレッチフィルムとして好適である。This composition is useful as a constituent of the main resin layer of a composite film, and such a composite film is suitable as a stretch film for food packaging.
食品包装用ストレッチフィルムには、可塑化ポリ塩化ビ
ニル(以下PvCと略記する)のフィルムが主として使
われているが、可塑剤の食品への移行等の衛生上の問題
、焼却時に有毒ガスを発生する等の公害問題を有してい
る。このため、PvCフィルムに代わるものとして、エ
チレン−酢酸ビニル共重合体(以下EVAと略記する)
のフィルムが販売されているが、PvCフィルムの代替
可能なしベルに達してい々い。すなわち、EvA系フィ
ルムは伸びやすくするため忙酢酸ビニル含量を増やせば
弱く破れやすくなり、それを防ぐために、フィルム厚み
を例えば/lμからコOμ、25μと増していくと、又
伸びic<くなる。又、酢酸ビニル含量を増やすと、フ
ィルムはゴム的々弾性挙動を示すようKなり、フィルム
同志の粘着・シールがで1力〈なり、又、厚みの増加は
コスト的にも不利である。Plasticized polyvinyl chloride (hereinafter abbreviated as PvC) film is mainly used as stretch film for food packaging, but there are hygienic problems such as the transfer of plasticizer into food, and the generation of toxic gas when incinerated. There are pollution problems such as Therefore, as an alternative to PvC film, ethylene-vinyl acetate copolymer (hereinafter abbreviated as EVA) is used.
There are several films on the market, but the ability to replace PvC film has not yet reached its potential. In other words, if you increase the vinyl acetate content to make the EvA film easier to stretch, it will become weaker and more likely to tear, and to prevent this, if you increase the film thickness from /lμ to 0μ to 25μ, the elongation will become ic<. . In addition, when the vinyl acetate content is increased, the film exhibits elastic behavior similar to rubber, and the adhesion and sealing between the films becomes weaker, and the increased thickness is also disadvantageous in terms of cost.
このようか相反する問題点を解決するストレッチフィル
ムに適する組成物として、例えば、EVA。An example of a composition suitable for a stretch film that solves these contradictory problems is EVA.
エチレン−α−オレフィン共重合体ニジストマー1ポリ
プロピレンの三元組成物を開示する特公昭39−319
76号公報があり、又、フィルムとしては特開昭tO−
79932号公報の発明がある。そして、このフィルム
は従来のオレフィン系ストレッチフィルムに較べて極め
て高い耐熱性、ヒートシール性、ストレッチ性を有する
フィルムであった。Japanese Patent Publication No. Sho 39-319 disclosing a ternary composition of ethylene-α-olefin copolymer nidistomer 1 polypropylene
No. 76, and as a film, JP-A-Shoto-O-
There is an invention disclosed in Publication No. 79932. This film had extremely high heat resistance, heat sealability, and stretchability compared to conventional olefin stretch films.
近年、ストレッチ包装の分野において、機械化や多様化
が進んでいる。包装の主流は従来のハントラッパーを用
いるハンド包装から、省力化、高速化が可能な機械包装
へ移行している。又、機械包装においても、以前は機械
調整(例えばストレッチ率等)を十分性なった後に特定
の被包装物を大量に包装する方式がとられていたが、最
近では多種多様の材質、形状のトレーを少量ずつ機械調
整をほとんどせず、ランダムに包装する方式に変化して
いる。又、フィルムが破れやすい突起を有した被包装物
(カニのハサミ、冷凍魚等)の包装も機械で行なわれる
ようKなり、ストレッチフィルムには、このような汎用
性の要求が極めて高いものとなっている。In recent years, mechanization and diversification have progressed in the field of stretch packaging. The mainstream of packaging is shifting from traditional hand packaging using hand wrappers to machine packaging, which can save labor and increase speed. In addition, in the past, mechanical packaging used to involve packaging specific items in large quantities after making sufficient machine adjustments (e.g., stretch rate), but in recent years, a wide variety of materials and shapes have been used. The method has changed to packaging trays in small quantities at random, with little mechanical adjustment. In addition, machines are now used to package items that have protrusions that can easily tear the film (crab scissors, frozen fish, etc.), and stretch films are now required to have such versatility. It has become.
特公昭39−3t97A号公報等に開示されている従来
の組成物では、フィルムに成形してもその汎用性が十分
で々く、多種多様な材質や形状のトレーのランダム包装
に適応できないという問題点があり、特殊な被包装物に
ついては包装不能であった。又、この組成物を主体とし
て用いる場合には、延伸、脱配向等の条件を変えてフィ
ルムの物性を高めようとすると偏肉が悪化し、製膜性が
低下するという問題点があった。Conventional compositions disclosed in Japanese Patent Publication No. 39-3T97A etc. have sufficient versatility even when formed into a film, and cannot be applied to random packaging of trays made of a wide variety of materials and shapes. There were some points, and it was impossible to package special items. In addition, when this composition is used as a main component, there is a problem in that if the physical properties of the film are attempted to be improved by changing conditions such as stretching and deorientation, thickness unevenness worsens and film formability deteriorates.
1間険点を解決するだめの手段〕
本発明者は、ストレッチ包装における機械包装適性、そ
の汎用性を向上すべく鋭意研究を行なった結果、低密度
ポリエチレン、又は特定のエチレン共重合体類と超低密
度ポリエチレンと結晶性ポリオレフィンの3成分の特定
配合割合からなる三元組成物が優れた冷間延伸性を有す
ることを見い出し、又、成形されたフィルムは伸びやす
きと破れにくさという相反する性質が著しく改善され、
その包装性は卓越した汎用性と仕上がりの美しさを持つ
ことを見い出して、本発明に到達したものである。As a result of intensive research to improve the mechanical packaging suitability and versatility of stretch packaging, the present inventor discovered that low-density polyethylene or specific ethylene copolymers It was discovered that a ternary composition consisting of a specific blending ratio of three components, ultra-low density polyethylene and crystalline polyolefin, has excellent cold stretchability, and the formed film has the contradictory properties of being easy to stretch and difficult to tear. properties are significantly improved,
The present invention was developed based on the discovery that the packaging property is excellent in versatility and has a beautiful finish.
す々わち本発明は、(A)低密度ポリエチレン、エチレ
ン−酢酸ビニル共重合体、エチレン−アクリル酸エチル
共重合体、エチレン−アクリル酸共重合体、アイオノマ
ー樹脂より々る群から選ばれる少なくとも7種の重合体
、(B)密度がQ9/り/−以下、融点llO″C以上
、7%モジュラスがlOO〜/ 000We−rl−よ
−
の超低密度ポリエチレン、(C)結晶性ポリプロピレン
、結晶性ポリブテン−7のいずれか、又はこれらの混合
物、である(2)、(Bl及び(C)の樹脂混合物で、
(A)、(8)、(C’)の混合重量比が0.90≧B
/(A+B)≧a、io。In other words, the present invention provides at least one material selected from the group consisting of (A) low density polyethylene, ethylene-vinyl acetate copolymer, ethylene-ethyl acrylate copolymer, ethylene-acrylic acid copolymer, and ionomer resin. 7 types of polymers, (B) ultra-low density polyethylene with a density of Q9/li/- or less, a melting point of 11O"C or more, and a 7% modulus of 100~/000We-rl-, (C) crystalline polypropylene, Any of crystalline polybutene-7 or a mixture thereof, (2), a resin mixture of (Bl and (C)),
The mixing weight ratio of (A), (8), and (C') is 0.90≧B
/(A+B)≧a, io.
aSO≧C/(A+B)≧O,OSであるフィルム成形
用樹脂組成物に関するものである。The present invention relates to a film-molding resin composition in which aSO≧C/(A+B)≧O, OS.
以下に図面等を用いて本発明の詳細な説明する。The present invention will be described in detail below using the drawings and the like.
第一図は本発明の組成物を主体としたフィルムを製造す
るのに好適なプロセスの1例を示す概念図である。第一
図に従って具体的にこのプロセスを説明する。FIG. 1 is a conceptual diagram showing an example of a process suitable for producing a film mainly composed of the composition of the present invention. This process will be explained in detail according to FIG.
(1)、(1′)、(1′1の3台の押出機を用意し、
うち7台には本発明組成物をベース層用として供給し、
他の一台には耐熱層(H層)用樹脂と、スキン層(8層
)用樹脂を配し、環状ダイ(2)よυ合体させチューブ
状に押出す。この際、ダイ(2)内において、S層/ペ
ース層/H層/S層、S層/ベースN/H層/ベース層
/S層等の多層に重ね合わせ、押出されたチューブは水
冷リング(3)により急冷され、7対のピンチロール(
A)により折り畳んで原反を得る。原反はコ対のピンチ
ロール(5)、(Aの間で、内部にエアを入れ、ひねる
ことにより偏肉を分散させ延伸機に送られる。λ対のピ
ンチロール(6)、cIolの間で、加熱リング(8)
、熱風循環ゾーン(γ)でqO〜qo”cの延伸湿度(
バブルの延伸開始点の温度)まで加熱し、エアの内圧に
より膨張させバブルを作りニアリング(9)、<i>
Kより−O°C程度に冷却し、冷間延伸を付与し、デフ
レータ−で折り畳み、ピンチロールaυで引き取ってフ
ィルムを得る。これをヒートセット装置(川により熱風
で加熱・収縮させ、巻取機(ロ)において一枚のフィル
ムに分けて巻き取り、製品を得る。Prepare three extruders: (1), (1'), (1'1),
Seven of them were supplied with the composition of the present invention as a base layer.
In the other machine, the resin for the heat-resistant layer (H layer) and the resin for the skin layer (8 layers) are arranged, and they are combined by the annular die (2) and extruded into a tube shape. At this time, in the die (2), multiple layers such as S layer/paste layer/H layer/S layer, S layer/base N/H layer/base layer/S layer are stacked, and the extruded tube is placed in a water-cooled ring. (3) and then 7 pairs of pinch rolls (
The original fabric is obtained by folding according to A). The raw fabric is passed between a pair of pinch rolls (5) and (A) by introducing air inside and twisting to disperse uneven thickness, and then sent to a stretching machine. And heating ring (8)
, the stretching humidity (
The process is heated to the temperature at which the bubble begins to stretch, and is expanded by the internal pressure of air to form a bubble, nearing (9), <i>
The film is cooled to about -0°C from K, subjected to cold stretching, folded with a deflator, and taken off with pinch rolls aυ to obtain a film. This is heated and shrunk with hot air by a heat setting device (river), and is divided into a single film and wound up in a winding machine (b) to obtain a product.
従来、第一図の冷間延伸のプロセスにおいて、加熱温度
SO″C以下で延伸を行がう場合、フィルムの応力が高
く、柔軟性が不十分であるという欠点を持っていた。又
、第2図のプロセスは、加熱湿度60℃以上の延伸には
、一般に不安定であった。Conventionally, in the cold stretching process shown in Figure 1, when stretching is carried out at a heating temperature of SO''C or lower, the stress of the film is high and the flexibility is insufficient. The process shown in Figure 2 was generally unstable for stretching at heating humidity of 60° C. or higher.
次に1本発明の樹脂組成の範囲を第2図により説明する
。Next, the range of the resin composition of the present invention will be explained with reference to FIG.
第1図は後に示す実施例/及び比較例/のNa/〜/4
Cに対応する実験解析図である。Figure 1 shows Na/~/4 of Examples/and Comparative Examples/ shown later.
It is an experimental analysis diagram corresponding to C.
図中、成分囚は低密度ポリエチレン、EVAN xチレ
ンーアクリル酸エチル共重合体、エチレン−アクリル醗
共重合体、アイオノマー樹脂のいずれか、又は、これら
の混合物である。低密度ポリエチレンはメルトインデッ
クスC以下MIと略す)aコル10.密度Q9/ −(
19J 9/aAのものである。エチレン共重合体類は
エチレン以外の単量体の量が一〜l−モルチ、MI(l
λ〜1oのものである。これらの中で高圧法によシ製造
された低密度ポリエチレン、EVAが好ましい。In the figure, the components are low density polyethylene, EVAN x tyrene-ethyl acrylate copolymer, ethylene-acrylic copolymer, ionomer resin, or a mixture thereof. Low-density polyethylene has a melt index of C or below (abbreviated as MI) a Col 10. Density Q9/-(
19J 9/aA. Ethylene copolymers contain monomers other than ethylene in an amount of 1 to 1 molar, MI (l
λ~1o. Among these, low-density polyethylene and EVA produced by a high-pressure method are preferred.
成分(B)の超低密度ポリエチレンとは、プラスチック
・エンジニアリング第1/巻、P、Jり〜ぶコ(lrj
))に記載されているものであり、エチレンと炭素数3
〜1個のα−オレフィンとの共重合体である。The ultra-low density polyethylene of component (B) is described in Plastic Engineering Volume 1/P, J Ribuco (lrj
)), which contains ethylene and 3 carbon atoms.
It is a copolymer with ~1 α-olefin.
成分(Oの結晶性ポリプロピレン、結晶性ポリブテンと
け、アイソタクシティの高い結晶性ポリマーであり、ポ
リプロピレンはプロピレンの単独重合体、又は、プロピ
レンと7モルチ以下のα−オレフィンとの共重合体を含
むもので、MI(l N2Qのものである。ポリブテン
は低分子量の液状、ワックス状のものと実なりブテン−
/含量93モル%以上で、他のモノマーとの共重合体を
も含む高分子量のものである。Crystalline polypropylene with crystalline polybutene (O) is a crystalline polymer with high isotacticity. It is a product of MI (l N2Q).Polybutene is a low molecular weight liquid, waxy type, and fruit butene-
It has a high molecular weight content of 93 mol% or more and also contains copolymers with other monomers.
第1図の座標系を説明すると、頂点A、B、Cは各々の
成分が100%であることを示し、辺AB上では、成分
(C)が0%で、成分(A)と(B)の比率は頂点AK
近づくほど成分囚が多いことを示している。To explain the coordinate system in Figure 1, vertices A, B, and C indicate that each component is 100%, and on side AB, component (C) is 0%, and components (A) and (B ) is the ratio of apex AK
The closer you get, the more prisoners there are.
又、辺ABとの平行線は頂点Cに近づくにつれて、成分
(C)が70%、20%、30% と増えることを示し
ている。例えば、点イ(J41.291.!i)は成分
■47重量%、成分(n)x9重量%、成分(C) 3
重量%であることを示してい石。Further, a line parallel to side AB indicates that as it approaches vertex C, component (C) increases by 70%, 20%, and 30%. For example, point A (J41.291.!i) has component ■47% by weight, component (n) x 9% by weight, and component (C) 3
Shows the weight percentage of the stone.
図中に記した◎、01△、×の記号は、上記(A)、(
B)、(C)の3成分組成のもたらす各特性値、すなわ
ち、フィルムの製膜性を示す原反折幅変動、平均バブル
寿命、安定温度域、フィルム偏肉と、ストレッチフィル
ムとしての必要特性を示す。ヘイズ、落鍾衝撃強度、1
0O%伸び応力の計7つの特性に 9 一
ついて総合的に評価した結果を、囚、(B)、(C)各
成分の比率とともに座標系上にプロットしたものである
。総合評価が◎、○で衷わされる領域は、点イ (6に
、29、り、点0 (10,I#、り、点/S(7、
tO,!り、点二(37,20,33)に囲まれた範囲
にあり、その周辺に総合評価△、×の点が配置されてい
る。このようが解析により、点イロハニに囲まれた範囲
、す々わち、特許請求の範囲において、ストレッチフィ
ルムとして有用な組成物を与えることがわかった。The symbols ◎, 01△, and × in the figure are (A), (
Characteristic values brought about by the three-component composition of B) and (C), namely, the fluctuation of the folded width of the original film indicating the film formability, the average bubble life, the stable temperature range, the uneven thickness of the film, and the necessary characteristics as a stretch film. shows. Haze, falling impact strength, 1
The results of a comprehensive evaluation of a total of seven properties of 00% elongation stress are plotted on a coordinate system along with the ratio of each component (B) and (C). The areas where the overall evaluation is ◎, ○ are points A (6, 29, ri, points 0 (10, I#, ri, points/S (7,
tO,! It is in the range surrounded by point 2 (37, 20, 33), and points with comprehensive evaluations Δ and × are arranged around it. It has been found through analysis that the area surrounded by the dots, ie, the claims, provides a composition useful as a stretch film.
後に掲げる第3表は本発明組成物と従来の特公昭19−
31976号公報の組成物の比較を、組成物の製膜条件
とその条件における特性について示している。第3表に
よると、本発明組成物は第2図に示す如き冷間延伸のプ
ロセスにおいて、従来の組成物では成し得なかった温度
範囲での延伸が極めて安定である。その結果として1本
組成物から得られたフィルムは、従来組成の冷間延伸で
は同時1cII足することが不可能であった、寸法安定
性、偏肉、柔軟性のすべてを満足するものであった。Table 3 listed below shows the composition of the present invention and the conventional Japanese Patent Publication No. 1973-
A comparison of the compositions of No. 31976 is shown in terms of the film forming conditions of the compositions and the properties under those conditions. According to Table 3, the composition of the present invention is extremely stable in the cold stretching process shown in FIG. 2 in a temperature range that cannot be achieved with conventional compositions. As a result, the film obtained from one composition satisfies all of the requirements of dimensional stability, uneven thickness, and flexibility, which was impossible to simultaneously add 1cII by cold stretching with the conventional composition. Ta.
第q表はフィルムの機械包装適性、その汎用性を示した
ものである。第弘表によると本組成物により得られるフ
ィルムは、実際に市場において問題とがりがちな特殊な
内容物の包装、又、多種多様な材質、形状のトレー包装
に十分適応しており、他のフィルムより優れた包装の仕
上がり、汎用性を示している。このことは、本組成物な
用いたフィルムの高い実用性を示している。Table Q shows the film's suitability for mechanical packaging and its versatility. According to Table 1, the film obtained from this composition is well suited for packaging special contents that tend to be problematic in the actual market, as well as for tray packaging of a wide variety of materials and shapes. It shows superior packaging finish and versatility. This indicates the high practicality of the film used with this composition.
以下に実施例を挙げて本発明の詳細な説明する。 The present invention will be explained in detail by giving examples below.
なお、実施例中の測定、評価は下記の方法によった。Note that measurements and evaluations in the examples were carried out by the following methods.
(評価方法)
/)原反折幅変動
原反の折幅を2Q11にわたって連続的に測定し、その
最大と最小の差R(m)を平均折幅で割り、100倍し
た値。(Evaluation method) /) Folding width variation of original fabric The folding width of the original fabric was measured continuously over 2Q11, and the difference between the maximum and minimum R (m) was divided by the average folding width and multiplied by 100.
◎ ぐ%未満
○ tI%以上 7%未満
Δ 7%以上 10%未満
x io%以上
コ)平均バブル寿命
r時間の製膜テストを最適延伸条件で行なった際の平均
パズル持続時間。◎ Less than 7% ○ tI% or more but less than 7% Δ 7% or more and less than 10%
◎ 一時間以上
01時間以上 2時間未満
△ 30分以上 1時間未満
× 30分未満
3)安定延伸温度域
安定に延伸ができる延伸温度範囲。製膜テストを行ない
、30分以上のバブル寿命を有し、かつ−バブルのゆれ
のない条件を安定な延伸温度とした。◎ 1 hour or more 1 hour or more Less than 2 hours △ 30 minutes or more Less than 1 hour × Less than 30 minutes 3) Stable stretching temperature range A stretching temperature range that allows stable stretching. A film forming test was conducted, and conditions were defined as a stable stretching temperature that had a bubble life of 30 minutes or more and had no bubble fluctuation.
◎ コO℃より大きい
○ 10’Cより大きく20′C以下Δ 3℃より太
きく10′C以下
x t’c以下
Il) フィルム偏肉
フィルムの幅方向Kj Otwa間隔でvO点厚みを測
定し、これを流れ方向に3回繰り返しだとき、その平均
厚みからの厚薄を±X%として表わした。◎ Greater than 0℃ ○ Greater than 10'C and less than 20'C Δ Greater than 3℃ and less than 10'C When this was repeated three times in the machine direction, the thickness from the average thickness was expressed as ±X%.
◎ 3%以下 ○ 3%より大きくio%以下 Δ 10%より大きく20%以下 X 20%より大きい j) ヘイズ値 ASTM−D −10(:)J−sコによね測定した。◎ 3% or less ○ More than 3% and less than io% Δ Greater than 10% and less than 20% X greater than 20% j) Haze value Measured according to ASTM-D-10 (:) J-sco.
◎ /、0%以下
0 /、0%より大きく2%以下
Δ 20%より大きく3%以下
×3.0%よシ大きい
乙)落鍾衝撃強度(以下ダート強度と略す)フィルムの
破れやすさに対する強度の尺度として用いた。ASTM
−D−/709−47法に準じて測定した。◎ /, 0% or less 0 /, greater than 0% and less than 2% Δ Greater than 20% and less than 3% It was used as a measure of strength against. ASTM
-D-/Measured according to method 709-47.
◎ 3QKgcm以上
○ j OKg cmm以上30K譚譚満△ / OK
y am以上、20Kgcm未満X 10Kgcm未
満
7) ioo%伸び応力
フィルムの伸びやすさ、柔軟性の尺度として用いた。A
STM−D−112−t7法に準じたす[張試験を行な
い、10O%伸び時の応力(VI。◎ 3QKgcm or more ○ j OKg cm or more 30K Tantan △ / OK
y am or more, less than 20 Kgcm x less than 10 Kgcm 7) ioo% elongation Used as a measure of ease of stretching and flexibility of the stress film. A
A tensile test was conducted according to the STM-D-112-t7 method, and the stress at 100% elongation (VI.
■幅)を表わしたもので、タテ、ヨコの平均値で示した
。■Width), expressed as the average value of vertical and horizontal values.
◎ コ”’JI10tm幅以下
0 −2009/10mmより大2!Og/1(Ha
s幅以下△ 、2jOg/1O1a1幅より大300
g/lo■幅以下X 3009/10wx幅より大
t)総合評価
上記7項目について、◎を3点、○を2点、Δを1点、
×を0点として合計点によシ評価した。◎ JI10tm width or less 0 -2009/Large than 10mm2!Og/1(Ha
s width or less △, 2jOg/1O1a1 width greater than 300
g/lo ■ Width or less
Evaluation was made based on the total score, with × as 0 points.
◎ /r点点上 上 /グ点以上 77点以下 Δ 10点以上 13点以下 × 9点以下 実施例に使用した樹脂のリストを以下に記す。◎ /On point r Upper/G point or higher, 77 points or lower Δ 10 points or more 13 points or less × 9 points or less A list of resins used in the examples is shown below.
ml : E V A (酢酸ビニル含量j、 j モ
# %、MI/、o)ILz:EVA(酢酸ビニル含量
!、jモルチ、M工/、0)a3:低密度ポリエチレン
(LDPE)(Ml、2.O,密度aqirり/al
、 m、p、 /(7,r℃〕a4: エチレン−
アクリル酸エチル共重合体(EEA)〔アクリル酸エチ
ル含量S、Oモル%、MI/、t)as;アイオノマー
樹脂(IO) (エチレン−メタアクリル酸共重合体N
a中和タイプ、メタアクリル酸含量7.4モル%、MI
/、(7,中和度コ!%、ケン化度!O%〕b1:超低
密度ポリエチレy(ULDPE)(密度arq9/al
、MI Qlr、ユニオン・カーバイト社製ニーカーフ
レックスDEFD−tx / ONT )
b、 i UI、DPE (密度Q90り/cl!、M
Ia+、ユニオy’カーバイト社製ニーカーフレックス
I)FDA−/131NT)el ’結晶性ポリプロピ
レン(IPP)(エチレンをくを重量Sランダム共重合
したもの、MFR7,0,m、p、 / / 7°C〕
c2:結晶性ポリブテン(PB−/)Cブテン−/含量
9gモルチ、密度o、qosり/cJ、MI/、0)a
s : I PP (MFR2,,2、密度aqig
t〆一、m、 p、 /l’l”(,1実施例/及び比
較例1
エチレン−酢酸ビニル共重合体(EVA)(ILI )
20重量%に、超低密度ポリエチレン(ULDPE)
(bt )4層重量%と結晶性ポリプロピレン(IPP
)(Cx)/j重量%を混合し、ペース用として用意し
た。又、次K IPP(Ct) I 0重量%と結晶性
、i’ IJブテン(PB/)(e2)20重量%を混
合しH層剤として、EVA(a2)を8層用として、第
一図に示すプロセスを用いて延伸、製膜した。ml: EV A (vinyl acetate content j, j mo # %, MI/, o) ILz: EVA (vinyl acetate content!, j morch, M engineering/, 0) a3: low density polyethylene (LDPE) (Ml, 2.O, density aqir/al
, m, p, / (7, r℃] a4: ethylene-
Ethyl acrylate copolymer (EEA) [ethyl acrylate content S, O mol%, MI/, t) as; ionomer resin (IO) (ethylene-methacrylic acid copolymer N
a Neutralized type, methacrylic acid content 7.4 mol%, MI
/, (7, degree of neutralization !%, degree of saponification! 0%) b1: Ultra low density polyethylene (ULDPE) (density arq9/al
, MI Qlr, Union Carbide Knee Car Flex DEFD-tx/ONT) b, i UI, DPE (Density Q90/cl!, M
Ia+, Unio Y'Carbide Nycarflex I)FDA-/131NT)el'Crystalline polypropylene (IPP) (weight S random copolymerization of ethylene, MFR7,0,m,p,//7 °C]
c2: Crystalline polybutene (PB-/)C butene-/content 9g molti, density o, qosr/cJ, MI/, 0) a
s: I PP (MFR2,,2, density aqig
t〆1, m, p, /l'l'' (, 1 Example/and Comparative Example 1 Ethylene-vinyl acetate copolymer (EVA) (ILI)
20% by weight, ultra low density polyethylene (ULDPE)
(bt) 4 layer weight% and crystalline polypropylene (IPP
)(Cx)/j% by weight was mixed and prepared as a paste. In addition, 0% by weight of the next K IPP (Ct) I and 20% by weight of crystalline, i' IJ butene (PB/) (e2) were mixed as the H layer agent, EVA (a2) was used as the 8 layer agent, and the first It was stretched and formed into a film using the process shown in the figure.
この際、ベース層用押出機に添加剤として、ジグリセリ
ン・モノオレエート、ポリオキシエチレン・ノニル・フ
ェニル°エーテル、ミネラル・オイルを各々1.!r*
−flkチ、/、3重量%、/、0重量%の計弘重量%
を注入、混練した。At this time, diglycerin monooleate, polyoxyethylene nonyl phenyl ether, and mineral oil were added to the extruder for the base layer as additives. ! r*
-Flk Chi, /, 3 wt%, /, 0 wt% total weight%
was injected and kneaded.
又、原反の厚み構成は、第1層、第5層が8層で各々7
μ、第2層、第μ層がベース層で各々−弘、jμ、第3
層がH層で7μ、j層合計で70μであった。In addition, the thickness of the original fabric is 8 layers for the 1st layer and 5th layer, and 7 layers each.
μ, the second layer, and the μ-th layer are the base layers, respectively.
The thickness of the H layer was 7μ, and the total thickness of the J layer was 70μ.
延伸温度70℃において、タテ2.2〜2.11倍、ヨ
コ3.Il〜3.を倍に延伸させ、ヒートセット装Nω
)において3o″Cの熱風を吹き付け、タテj%−ヨコ
j%収縮させた後、フィルムを得た。At a stretching temperature of 70°C, the length is 2.2 to 2.11 times, and the width is 3. Il~3. Stretch it twice and heat set Nω
) was blown with hot air at 3o''C to shrink the film by j% vertically and j% horizontally, and then a film was obtained.
これをNll/とする。又、第1表に示すような囚、(
B) 、(C)各成分のポリマーの種類、比率を変えた
ベース層用組成を用いて、N11/と同様に第2図に示
すプロセスでフィルムを得た。Let this be Nll/. Also, prisoners as shown in Table 1 (
B) and (C) Films were obtained by the process shown in FIG. 2 in the same manner as N11/, using base layer compositions in which the types and ratios of the polymers of each component were changed.
第2表に実施例/(NIL/〜r)と比較例/ (m
9〜z&)の延伸製原性と物性を前記ハ〜r)の方法に
より評価し、その結果を示す。Table 2 shows Example/(NIL/~r) and Comparative Example/(m
The stretching properties and physical properties of Samples 9 to z&) were evaluated by the methods of c to r) above, and the results are shown below.
以下K、第2表に基づいて、(A)、(B)、(Q各成
分の役割を考察すると、次のように々る。Based on Table 2 below, the roles of each component (A), (B), and (Q) are considered as follows.
成分(A)は押出性、透明性等を改良しており、嵩7と
隠/ノの比較でも明らかなように、成分(B)との比率
が70重量%以下になると、ドローレゾナンス(引取共
鳴)々る現象が発生し、原反の折幅変動が急激に劣化し
、後の延伸が不能となってしまう。Component (A) improves extrudability, transparency, etc., and as is clear from the comparison of bulk 7 and concealment/no, when the ratio with component (B) is 70% by weight or less, draw resonance Resonance) phenomenon occurs, and the fold width fluctuation of the original fabric deteriorates rapidly, making subsequent stretching impossible.
成分(B)は衝撃強度・柔軟性、透明性を改良しており
、成分(A)と(C)の相溶性を向上させ、相乗効果を
高める働きをもっている。成分(B)が少々い場合には
hrとに/μの比較かられかるように、相溶性の低下か
ら透明性が著しく低下し、衝撃強度、柔軟性も低いもの
となってし1う。Component (B) has improved impact strength, flexibility, and transparency, and has the function of improving the compatibility of components (A) and (C) and enhancing the synergistic effect. If component (B) is present in a small amount, transparency will be significantly lowered due to decreased compatibility, and impact strength and flexibility will also be lowered, as can be seen from the comparison of hr and /μ.
成分(C)はフィルムの腰、バブル安定性を改良してお
り1少々い場合にけN(L !;と漱10から明らかな
ように1バブル安定性が低下しパンクしやすく、偏肉の
悪いフィルムしか得ることができない。一方・成分(q
が多すぎる場合けNαλとH1l/ 、2から明らかな
ように1フイルムの柔軟性が低下し、ストレッチフィル
ムとして使用できない亀のとなってしまう。Ingredient (C) improves the firmness and bubble stability of the film, and as is clear from 10, when the film is slightly thinner, the 1-bubble stability decreases and punctures are more likely to occur, resulting in uneven thickness. Only bad films can be obtained.On the other hand, component (q
If there are too many, the flexibility of the film decreases as is clear from Nαλ and H1l/, 2, resulting in a film that cannot be used as a stretch film.
(以下余白)
−/r−
比較例−
ペース層組成物として、EVA(at)に3重量%、エ
チレン−α−オレフィン共共重合体熱可塑性シラス マ
ー 〔α−オレフィンがプロピレンで15モル%、エチ
リデンノルボルネン3重量%を共重合させたもノテ、M
I (lIl&、ビカット軟化点IIo℃以下〕(b3
)20重量%、IPP(et) 13重量%、PB−/
(es)3重量%を混合してベース層用組成とし、実施
例/と同様の方法で押出し原反を得た。(Left below) -/r- Comparative Example - As a paste layer composition, 3% by weight of EVA (at), ethylene-α-olefin copolymer thermoplastic silasmer [15% by mole of α-olefin in propylene, Monote, M copolymerized with 3% by weight of ethylidene norbornene
I (lIl&, Vicat softening point IIo℃ or less) (b3
) 20% by weight, IPP(et) 13% by weight, PB-/
(es) 3% by weight was mixed to prepare a base layer composition, and an extruded original fabric was obtained in the same manner as in Example.
コレラ延伸温度1.tt”cでタテ2.3倍、ヨコ3.
3倍に延伸させ、ヒートセット装置でタテS%、ヨコ3
%収縮させたものをAとした。又1延伸混度u s ”
Cで同様に延伸させた後、タテ/j%、ヨコ70%収縮
させたものをBとした。さらに1延伸温度70″Cで実
施例/とまったく同様の延伸、収縮処理をしたものをC
とした。Cholera stretching temperature 1. tt”c is 2.3 times vertical and 3 times horizontal.
Stretched to 3 times, length S%, width 3 using heat setting device
% shrinkage was designated as A. 1. Stretching mix us ”
After stretching in the same manner as in C, B was shrunk by 70% in the vertical direction and 70% in the horizontal direction. Furthermore, C
And so.
第3表に各種のフィルムの物性と延伸状態の結果を実施
例1の階/の結果とともに示す。Table 3 shows the results of the physical properties and stretching conditions of various films, together with the results of Example 1.
第3表によると、実施例1f)Nnlはフィルム応力も
低く、偏肉も優れ、寿命も3時間以上と極め一+2/−
で優れ、申し分かいものであった。According to Table 3, Example 1f) Nnl had low film stress, excellent thickness unevenness, and service life of 3 hours or more, which was extremely excellent at 1+2/-, and was satisfactory.
Aは、フィルムの偏肉、バブル寿命はまずまずだったが
、フィルムの応力が高いことと、<c o ”cKおけ
るフィルムの熱収縮率が高いため、製品として市場を流
通する間に1夏場々どは特に幅収縮を発生し商品として
は不十分のものであった。For A, the thickness unevenness and bubble life of the film were fair, but due to the high stress of the film and the high heat shrinkage rate of the film at In particular, width shrinkage occurred and the product was unsatisfactory as a commercial product.
Bは、比較例/の欠点を補うべく、ヒートセット装置に
おいてフィルムを大きく収縮させ、フィルム応力とμO
℃熱収縮率を引き下げたものである。しかし、ヒートセ
ットにおいて過大な収縮をさせるために1フイルムの偏
肉が低下してしまう欠点を持っている。又、製品の厚み
を一定にすると、後の収縮量が多いために延伸時のバブ
ルのフィルム厚みが著しく薄くなり、バブルの寿命が低
下してしまう。In order to compensate for the drawbacks of Comparative Example/B, the film is greatly shrunk in a heat setting device to reduce film stress and μO.
℃ The heat shrinkage rate has been lowered. However, it has the disadvantage that the uneven thickness of one film decreases due to excessive shrinkage during heat setting. Furthermore, if the thickness of the product is kept constant, the film thickness of the bubble during stretching becomes extremely thin due to the large amount of subsequent shrinkage, resulting in a reduction in the life of the bubble.
Cけ、実施例1と同じ条件で製膜しようと試みたものだ
が、バブルの安定性が著しく悪いため、偏肉の悪いフィ
ルムの断片がわずかに得られたのみであった。C. An attempt was made to form a film under the same conditions as in Example 1, but because the stability of the bubbles was extremely poor, only a few film fragments with poor thickness unevenness were obtained.
このように、実施例1のNa/のフィルムは、比lj−
較例A、BSCでは不可能であった。寸法安定性、偏肉
、柔軟性、安定製膜性のすべてを満足するものであった
。Thus, the Na/film of Example 1 could not be compared with Comparative Example A, BSC. It satisfied all of the requirements of dimensional stability, uneven thickness, flexibility, and stable film formability.
第 3 表
機械包装テスト例
実施例/のNIl/、Napと比較例λのB1市販のp
vcJ 及U EVAiのストレッチフィルムについて
機械包装テストを行なった結果を第弘表に示した。Table 3 Mechanical Packaging Test Examples Example/NIl/, Nap and Comparative Example λ B1 Commercially available p
Table 1 shows the results of mechanical packaging tests performed on stretch films of vcJ and U EVAi.
包装機械は直線型の大森機械工業■製5T−6090を
泪い、テストlとして、発泡ポリスチレン製標準型トレ
ーに内容物模擬の粘土を入れたものを包装した。テスト
コとして、つぶれやすいハイインパクトポリスチレン製
深型トレーに粘土を入れたものを包装した。テスト3と
して、トレーエツジでフィルムの破れやすい2軸延伸ポ
リスチレン製大型トレーに粘土を入れ包装した。テスト
gとして、仕上がりにシワの残りやすいサンマ包装用長
型トレーに粘土を入れ包装した。テスト!として、突起
のあるカニの爪を内容物として、テスト/と同様のトレ
ーで包装した。又、包装機械の調整はそれぞれのフィル
ムととにストレッチ率等のフィルムの張り調節をテスト
lで行々い、同じ条件でテスト2〜3を行かった。The packaging machine was a linear type 5T-6090 manufactured by Omori Machine Industry Co., Ltd. As test 1, a standard tray made of foamed polystyrene was filled with clay simulating the contents. As Testco, we packaged clay in deep trays made of high-impact polystyrene that are easy to crush. As Test 3, clay was placed and packaged in a large tray made of biaxially oriented polystyrene, where the film tends to tear at the tray edge. As test g, clay was placed in a long tray for packaging saury that tends to leave wrinkles on the finished product. test! The content of crab claws with protrusions was packaged in a tray similar to Test/. In addition, the packaging machine was adjusted by adjusting the tension of each film, such as the stretch rate, in Test 1, and Tests 2 and 3 were conducted under the same conditions.
評価は、
◎ すべでうまく包装できたもの
〇 一部小さなシワやひずみのでたもの△ シワ、破れ
、トレ一つぶれのあるもの× 包装できなかったもの
とし、◎を3点、○を2点、Δを7点、×を0点として
総合評価した。The evaluation is as follows: ◎ Items that were packaged well in all cases 〇 Items with some small wrinkles or distortions △ Items with wrinkles, tears, or uneven treads Comprehensive evaluation was made with Δ as 7 points and x as 0 points.
第μ表より明らかなように1実施例1のNIl/、隠g
け比較例−のBと比べて、著しく包装の混層性が向上し
ており、市販PvCフィルムと比べて、同等以上の性能
を有していた。市販EVA系は他のフィルムに比べると
、破れやすく包装の総合評価も極めて低いレベルであっ
た。又、テストjのごとき機械における包装が極めて難
しい内容物についても、実施例1のk l、 NCL
&は優れた包装性を有していた。As is clear from Table μ, NIl/, hidden g of Example 1
Compared to Comparative Example B, the mixing properties of the packaging were significantly improved, and the performance was equivalent to or better than that of commercially available PvC films. Compared to other films, commercially available EVA films were easily torn and the overall evaluation of the packaging was at an extremely low level. In addition, for contents that are extremely difficult to package in a machine such as test j, k l of Example 1, NCL
& had excellent packaging properties.
(以下余白)
−2よ−
〔発明の効果〕
叙述のとおυ本発明の組成物は、優れた押出成形性と延
伸性を有するとともに1優れた柔軟性、衝撃強度特性、
引張強度特性・透明性を有するフィルムを得ることので
きる組成物である。又、このような組成のフィルムは、
ストレッチフィルムに要求される機械包装性を満たす効
果を有し、産業界に果たす役割は大きい。(Left below) -2- [Effects of the Invention] As stated above, the composition of the present invention has excellent extrudability and stretchability, as well as excellent flexibility, impact strength properties,
This is a composition that allows you to obtain a film with good tensile strength and transparency. In addition, a film with such a composition is
It has the effect of meeting the mechanical packaging properties required for stretch films, and plays a major role in industry.
第1図は、本発明の樹脂組成物の3成分組成の−g−
範囲を示す三角座榛図である。
第2図は、本発明組成物を主体とする複合フィルムを製
造するのに好適なプロセスの1例を示す概念図である。
特許出願人 旭化成工業株式会社
代理人弁理士 星 野 −透一7−FIG. 1 is a triangular diagram showing the -g- range of the three-component composition of the resin composition of the present invention. FIG. 2 is a conceptual diagram showing an example of a process suitable for producing a composite film mainly composed of the composition of the present invention. Patent applicant Asahi Kasei Industries Co., Ltd. Representative Patent Attorney Hoshino -Toichi 7-
Claims (1)
その混合重量比が 0.90≧B/(A+B)≧0.30 0.50≧C/(A+B)≧0.05 であるフィルム成形用樹脂組成物。 (A)低密度ポリエチレン、エチレン−酢酸ビニル共重
合体、エチレン−アクリル酸エチル共重合体、エチレン
−アクリル酸共重合体、アイオノマー樹脂からなる群か
ら選ばれる少なくとも1種の重合体。 (B)密度0.91g/cm^2以下、融点110℃以
上、1%モジユラス100〜1000Kg/cm^2の
超低密度ポリエチレン。 (C)結晶性ポリプロピレン、結晶性ポリブテン−1の
いずれか、又はこれらの混合物。(1) A mixed resin of the following (A), (B), and (C),
A resin composition for film molding whose mixing weight ratio is 0.90≧B/(A+B)≧0.30 and 0.50≧C/(A+B)≧0.05. (A) At least one polymer selected from the group consisting of low density polyethylene, ethylene-vinyl acetate copolymer, ethylene-ethyl acrylate copolymer, ethylene-acrylic acid copolymer, and ionomer resin. (B) Ultra-low density polyethylene with a density of 0.91 g/cm^2 or less, a melting point of 110°C or more, and a 1% modulus of 100 to 1000 Kg/cm^2. (C) Crystalline polypropylene, crystalline polybutene-1, or a mixture thereof.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61185811A JPH0788446B2 (en) | 1986-08-07 | 1986-08-07 | Resin composition for film molding |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61185811A JPH0788446B2 (en) | 1986-08-07 | 1986-08-07 | Resin composition for film molding |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6341550A true JPS6341550A (en) | 1988-02-22 |
JPH0788446B2 JPH0788446B2 (en) | 1995-09-27 |
Family
ID=16177305
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61185811A Expired - Fee Related JPH0788446B2 (en) | 1986-08-07 | 1986-08-07 | Resin composition for film molding |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0788446B2 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0196235A (en) * | 1987-10-09 | 1989-04-14 | Showa Denko Kk | Thermoplastic resin composition |
JPH0292943A (en) * | 1988-09-29 | 1990-04-03 | Du Pont Mitsui Polychem Co Ltd | Polyolefin composition and laminated body thereof |
US5389448A (en) * | 1990-08-13 | 1995-02-14 | W.R. Grace & Co.-Conn. | Blends of polypropylene and ethylene copolymer and films made from the blend |
US5674608A (en) * | 1989-07-28 | 1997-10-07 | W. R. Grace & Co.-Conn. | Double bubble process for making strong, thin film |
JP2009507107A (en) * | 2005-09-01 | 2009-02-19 | イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー | Soft polymer composition having improved high temperature properties |
CN110669292A (en) * | 2019-10-29 | 2020-01-10 | 中国石油化工股份有限公司 | Preparation method of toughened polypropylene resin |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58206647A (en) * | 1982-05-28 | 1983-12-01 | Mitsubishi Petrochem Co Ltd | Resin composition for extrusion molding |
JPS59182832A (en) * | 1983-04-01 | 1984-10-17 | Idemitsu Petrochem Co Ltd | Polyolefinic resin composition |
-
1986
- 1986-08-07 JP JP61185811A patent/JPH0788446B2/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58206647A (en) * | 1982-05-28 | 1983-12-01 | Mitsubishi Petrochem Co Ltd | Resin composition for extrusion molding |
JPS59182832A (en) * | 1983-04-01 | 1984-10-17 | Idemitsu Petrochem Co Ltd | Polyolefinic resin composition |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0196235A (en) * | 1987-10-09 | 1989-04-14 | Showa Denko Kk | Thermoplastic resin composition |
JPH0292943A (en) * | 1988-09-29 | 1990-04-03 | Du Pont Mitsui Polychem Co Ltd | Polyolefin composition and laminated body thereof |
US5674608A (en) * | 1989-07-28 | 1997-10-07 | W. R. Grace & Co.-Conn. | Double bubble process for making strong, thin film |
US5674607A (en) * | 1989-07-28 | 1997-10-07 | W. R. Grace & Co.-Conn. | Double bubble process for making strong, thin films |
US5389448A (en) * | 1990-08-13 | 1995-02-14 | W.R. Grace & Co.-Conn. | Blends of polypropylene and ethylene copolymer and films made from the blend |
JP2009507107A (en) * | 2005-09-01 | 2009-02-19 | イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー | Soft polymer composition having improved high temperature properties |
US7655731B2 (en) * | 2005-09-01 | 2010-02-02 | E.I. Du Pont De Nemours And Company | Soft polymer compositions having improved high temperature properties |
CN110669292A (en) * | 2019-10-29 | 2020-01-10 | 中国石油化工股份有限公司 | Preparation method of toughened polypropylene resin |
Also Published As
Publication number | Publication date |
---|---|
JPH0788446B2 (en) | 1995-09-27 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0699219B1 (en) | Ethylene copolymers having narrow composition distribution, their production and use | |
US4619859A (en) | Highly-oriented stretchable multilayer film and process for producing the same | |
EP0721967B1 (en) | Thermoplastic seal and wrapping film | |
US6172172B1 (en) | Polyolefin compositions and blown films obtained therefrom | |
JPH0639920A (en) | Biaxially oriented heat-shrinkable film | |
JP2000507645A (en) | Polyolefin compositions exhibiting balanced sealant properties and improved tensile stress and methods thereof | |
PL165144B1 (en) | Laminated products manufactured from mixtures of a poliolefin and ethylene/vinyl alcohol copolymers and a method for manufacturing shaped liminated products from mixtures of a polyolefin and ethylene/polyvinyl alcohol copolymenrs | |
EP0780214B1 (en) | Food packaging stretch film | |
AU2005307750B2 (en) | Elastomeric compositions with improved resistance to necking for high speed sheet extrusion applications | |
EP1546254A2 (en) | Polymer compositions for extrusion coating | |
JPS6341550A (en) | Resin composition for molding film | |
JP3463528B2 (en) | Foam cushioning sheet | |
WO2012098947A1 (en) | Stretch packaging film | |
JPH0147311B2 (en) | ||
JP3490926B2 (en) | Polyolefin stretch packaging film | |
JPS5938976B2 (en) | improved composition | |
JP2974198B2 (en) | Polyolefin-based shrink laminated film and method for producing the same | |
JP3497767B2 (en) | Polyolefin stretch packaging film | |
JP3746166B2 (en) | Polyolefin-based stretch packaging film | |
US6211295B1 (en) | Polyolefin compositions and blown films obtained therefrom | |
JP2014076543A (en) | Film for stretch packaging | |
EP1772260B1 (en) | Propylene-based multilayered wrapping film | |
JP4823663B2 (en) | Stretch film for food packaging | |
JPH07149962A (en) | Polyethylene resin composition for high-speed inflation film | |
WO1997020889A1 (en) | Polyolefin compositions and blown films obtained therefrom |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |