JPH0153184B2 - - Google Patents
Info
- Publication number
- JPH0153184B2 JPH0153184B2 JP57161284A JP16128482A JPH0153184B2 JP H0153184 B2 JPH0153184 B2 JP H0153184B2 JP 57161284 A JP57161284 A JP 57161284A JP 16128482 A JP16128482 A JP 16128482A JP H0153184 B2 JPH0153184 B2 JP H0153184B2
- Authority
- JP
- Japan
- Prior art keywords
- ethylene
- film
- foam
- stretching
- longitudinal direction
- 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
Links
Landscapes
- Laminated Bodies (AREA)
Description
本発明は緩衝効果、印刷性等の優れた縦方向に
熱収縮性を有する複合発泡材料に関する。
従来、熱収縮性を有する例えば発泡シート、フ
イルム等の発泡材料は、その原料をポリスチレン
を使用したものが主流をしめ、特にこれがビン等
の容器類の外装に用いることにより、破ビン防止
効果と緩衝効果を発揮するので有用な包装材料と
して周知である。
ところが、前記ポリスチレンからなる熱収縮性
を有する発泡シートもしくはフイルム等は、その
原料の特性から衝撃に弱く脆いものであり、例え
ばビン等の破ビン防止効果、緩衝効果等を有する
ラベル用として装着しても、その洗浄工程や充填
工程、更には輸送中に発泡材料が破損するという
欠点があり、又同材料表面に印刷を施こしても鮮
明に表出できず、その上発泡材料が層状になつて
部分的に剥離する等の現象がみられ問題となつて
いた。
この発明は、前記した問題点を解決するために
なされたものであり、縦方向に熱収縮性を有する
複合発泡材料として、エチレン含有量が1〜10モ
ル%のエチレン―プロピレン共重合体と、弾性改
質用重合体、及び発泡剤とを配合した組成物を製
膜し、しかる後縦方向に延伸させることにより縦
方向に熱収縮性を有する発泡材料に、縦方向に熱
収縮性を有する熱可塑性フイルムがラミネートさ
れたことを発明の要旨とするものであり、以下本
発明について詳述する。
本発明で使用するエチレン―プロピレン共重合
体は、通常エチレン含有量1〜10モル%、好まし
くは2〜6モル%のもので、このさい10モル%を
越えると製造された発泡材料がべたついてブロツ
キングを起し易くなつて好ましくなく、また1モ
ル%未満ではその性質がポリプロピレンに近す
ぎ、従つて延伸しても収縮率が小さく、熱収縮性
部材として不満足である上に発泡セルが破れて毛
羽立ち現象を起し易くなる。なお前記共重合体中
にはエチレンがランダムに入つているものが好ま
しい。この際、前記共重合体の使用量は効果の表
われる量を適宜に加えればよいが、好ましくは全
重合体量に対し50〜95重量%程度でよい。
次に本発明で使用する弾性改質用重合体は、発
泡材料の発泡セルに弾性を付与するために添加す
するもので、この重合体を添加しない場合は発泡
の際の内部圧力に耐えられず発泡セルが膨脹し易
くなるので微細な発泡構造のものが得られない。
この重合体は発泡時のセルに弾性を付与する性
質を有するものが好ましく、例示すれば低、中、
高密度ポリエチレン、ポリブテン、エチレン―酢
酸ビニル共重合体、エチレン―エチルアクリレー
ト、エチレン―1―ブテン共重合体、プロピレン
―1―ブテン共重合体、不飽和カルボン酸及びそ
の誘導体等の極性基を有する変性ポリオレフイ
ン、1:2型ポリブタジエン、直鎖状低密度ポリ
エチレン(L―L DPE)等が代表的なもので
ある。
この際、より好ましい弾性改質用重合体として
は、酢酸ビニル含有量3〜40重量%のエチレン―
酢酸ビニル共重合体、エチレン含有量85〜95モル
%(密度0.86〜0.91、結晶化度3〜20%)のエチ
レン―1―ブテンランダム共重合体等を例示でき
る。なおこの弾性改質用重合体の使用量は少なく
ともその効果が表われる量を加えればよく、好ま
しくは全重合体量に対し5〜50重量%程度でよ
い。
又、本発明で使用する発泡剤は、公知のもので
あれば如何なるものでもよく、適応可能な発泡剤
としてその種類を例示すると、揮発性のものとし
てペンタン、ブタン等、有機系のものとしてヒド
ラジン系、ニトロソ系、アゾ系等が、又、無機系
のものとして重炭酸ソーダ、炭酸アンモニア等が
ある。この際、より好ましい例としては前記アゾ
系発泡剤ではアゾジカルボンアミド、アゾビスイ
ソブチロニトリル等、無機系発泡剤では重炭酸ナ
トリウム、炭酸アンモン等の炭酸塩とクエン酸、
洒石酸等の有機酸とからなるものをあげることが
できる。なお、この発泡剤の使用量は少なくとも
その効果が表われる量を加えればよいが、エチレ
ン含有量1〜10モル%のエチレン―プロピレン共
重合体と、弾性改質用重合体との合計量(全重合
体量)100重量部に対し、0.2〜5重量部、更に好
ましくは0.5〜2重量部程度を例示できる。上記
発泡剤は本発明に係るエチレン―プロピレン共重
合体に直接ブレンドしたり、濃度の高い発泡剤を
含むマスターペレツトを加えてブレンドしたり、
予じめ前記共重合体中に発泡剤を適宜量練り込ん
で用いたりすればよく、その用法には特に制限は
ない。
なお、本発明では上記3者からなる成分の他に
適宜の添加剤や充填剤等を加えることもあり、例
えば滑剤、帯電防止剤等を必要に応じ加えて物性
の改善を図ることも適宜行い得、必要ならば顔料
を添加することにより希望する着色も可能であ
る。
次に本発明では、前記発泡材料の印刷性を改良
し、その表面状態の改良等を図るため、該発泡材
料にラミネート層を形成させるもので、このラミ
ネート層(スキン層ともいう)として用いる熱可
塑性フイルムとしては、一般に使用されている各
種の熱可塑性重合体からなるフイルムを例示でき
特に制限はない。これらの数例を示すと、ポリオ
レフイン系樹脂としては低、中、高密度ポリエチ
レン、ポリプロピレン及びその共重合体等、ポリ
アミド系樹脂、ポリエステル系樹脂、ポリビニル
系樹脂、エチレン―酢酸ビニル共重合体、エチレ
ン―1―ブテン共重合体等である。その中で特に
好ましい例は、前記本発明の発泡材料と同種の重
合体からなるもので、エチレン含有量1〜10モル
%のエチレン―プロピレン共重合体あるいは例え
ば酢酸ビニル含有量3〜40重量%のエチレン―酢
酸ビニル共重合体、エチレン含有量85〜95モル
%、密度0.86〜0.91g/cm3、結晶化度3〜20%の
エチレン―1―ブテンランダム共重合体等の弾性
改質用重合体を単品で、もしくはこれらのブレン
ド物として用いると、アンカーコート層の必要が
なく発泡材料と熱圧着により直接ラミネートが可
能であつて至極便利である。一方、異質の熱可塑
性フイルムを用いると、屑等を回収して再利用す
ることが困難な場合も考えられるが、勿論利用は
可能である。なおラミネート層を形成する熱可塑
性フイルムも前述発泡材料と同様に、適宜の添加
剤や充填剤等を加えることもあり、例えば滑剤、
帯電防止剤等を必要に応じ加えて物性の改善を図
ることも適宜行い得、必要ならば顔料を添加する
ことにより希望する着色も可能である。
本発明に係る複合発泡材料とは、フイルム、シ
ート状のもの等の発泡材料に熱可塑性フイルムを
ラミネートしたものを例示でき、特にその形状を
限定するものでないが、フイルムやシート状のも
のは延伸操作が容易に出来るので好適な一例であ
る。
本発明は上記各成分を配合した発泡材料用、ま
たは熱可塑性フイルム用の組成物を製膜し、しか
る後、縦方向に延伸が行なわれる。こゝで縦方向
に延伸を行なうのは縦方向に熱収縮性を付与する
ためであり、これは発泡材料を製造する方向、即
ち縦方向に延伸を行なうことにより達成される。
また、本発明はフラツト状発泡材料を速度の異
なるロール間を通して行なう、いわゆるロール延
伸により縦延伸すれば最も好ましい結果が得られ
る。
この際、ロール延伸の具体例としては数個の等
速の予熱ロールを通して延伸可能な温度に予熱し
しかる後、所定の延伸比に設定された延伸ロール
により所望の倍率に延伸される方法を例示でき
る。
斯る予熱ロール温度は適宜でよいが好ましくは
90〜130℃に設定するとよい。高過ぎると低温収
縮性が損われ、収縮時に高い温度が必要になつ
て、エネルギーの損出が起こり、また部分的にシ
ートが溶融するという問題を生じたり、低すぎる
と延伸時に大きな応力が生じ、機械負荷が増大し
たり破れが生ずることもあり、好ましいとは言い
難いが実施は可能である。
前記した延伸ロールは適宜でよいが、一般に予
熱ロールより低く例えば60℃以下に設定されてお
り、こゝで延伸されたシートは数本の冷却ロール
により段階的に降下せしめ、常温として自然収縮
が起こりにくいようにすることも1方法である。
以上はフラツト状フイルムを例にとつて説明し
たが、一方チユーブラー状のものは複合化がしに
くい面はあるが実施は可能である。
この際、通常のインフレーシヨン方式で縦延伸
を行なうと横方向に若干配向の起ることも考えら
れるが、これらは全て本発明の範囲であり、フラ
ツト状のものも同様である。
その他縦延伸手段は前記のものに限定されるも
のでない。
次に本発明の複合発泡材料を作成する1例とし
て、押出機によりフイルムもしくはシート状に製
膜し、次いで熱可塑性フイルムを溶融押出ラミネ
ートして、ラミネート層を形成した後縦延伸する
方法を以下述べる。
先ず、エチレン含有量1〜10モル%のエチレン
―プロピレン共重合体と、弾性改質用重合体及び
発泡剤を配合した組成物をダイス内で発泡しない
程度に押出形機の条件設定を行い、ダイスからフ
ラツトのシート状に押出せる。そしてこの際同時
に発泡するようにすれば好適である。一方では前
記発泡材料の原料組成物と同種のエチレン1〜10
モル%のエチレン―プロピレン共重合体と弾性改
質用重合体とからなる熱可塑性樹脂配合物を押出
すと同時に、前記発泡材料(発泡シート)上に溶
融押出してラミネートし、熱可塑性フイルムによ
るラミネート層を形成する。
この際、熱可塑性フイルムはその押出しの際の
熱のため簡単なニツプロールにより発泡シートと
容易に積層一体化する。次いでロール延伸により
縦方向に延伸させるが、この延伸により発泡シー
トと熱可塑性フイルムがより強力に接着し、両者
はあたかも一層のシートとなり、極めて剥離し難
いものとなる。次に延伸温度(予熱温度を含め)
であるが、これは適宜選択できるが例えば90〜
130℃が好ましい。また、延伸倍率は必要に応じ
その大きさを選定するが、2倍以上、要すれば3
〜8倍程度に延伸すればよく、上記の各数値条件
で延伸を行えば好ましい縦方向の熱収縮性を有す
る複合発泡材料が得られるが、本発明は勿論これ
を限定するものではない。このようにして複合発
泡材料が作成されるのであり、この際、発泡材
料、熱可塑性フイルムの厚さは用途に応じて適宜
選択すればよい、また印刷性の向上を図るため熱
可塑性フイルムの表面にコロナ放電処理等の表面
処理を施すことも自由である。
以上は発泡材料(発泡シート)上に同種の熱可
塑性フイルムを溶融押出ラミネートする方法であ
るが、この他に同種の熱可塑性フイルムを予じめ
製膜しておき、発泡シートがダイスから押出し、
発泡したと同時に、該フイルムを発泡シート上に
ニツプロール等により押圧してラミネートしても
よい。この際発泡シート側に押出しの際の熱が残
つているため、両者は極めて容易に積層一体化で
きる。また発泡は製膜と同時が好ましいが、製膜
前であつても、製膜後であつても、更に延伸と同
時であつても差しつかえないことは勿論である。
以上は本発明に係る複合発泡材料を製造する好
ましい方法を述べたまでで、本発明はその他適宜
の方法を採ることも可能である。
本発明に係る複合発泡材料の用途としては、ビ
ン等に用いる印刷された外装用熱収縮性発泡ラベ
ルとして最も多用され、延伸方向がビン等の円周
方向と一致するように筒状化して用いればよいが
その他各種容器、各種物品の包装用材料として多
用され、その応用範囲は広く特に制限はない。こ
うした用途からみても複合発泡材料はシートもし
くはフイルム状態で用いることが最も好ましいわ
けである。
本発明は以上の通りであり、本発明に係る複合
発泡材料は例えばビン等の外装用ラベルとして用
いると、特に破ビン防止効果や緩衝効果に優れ
る。
また強度等の諸物性にも優れ従来のものゝ如く
脆くないので、例えば筒状体としても折りたゝむ
ことが可能で、折りたゝみの際に生じた折目は熱
収縮の際に消滅するという特性もある上に、材料
の端縁から層状となつて剥離し易いという欠点も
なく強靭である等の如く顕著な効果を奏する。以
下本発明の実施例を比較例と共に挙げる。
〈実施例 1〉
エチレン含有量4.5モル%のエチレン―プロピ
レンランダム共重合体70重量%と、酢酸ビニル含
有量15重量%のエチレン―酢酸ビニル共重合体
(弾性改質用重合体)30重量%の配合物100重量部
に対し、重炭酸ナトリウムとクエン酸の混合物か
らなる発泡剤1重量部を配合し、押出成型機のダ
イスを通してフラツトシート状押出し発泡させて
なる厚さ900μの発泡シートを作成した。
一方、エチレン含有量4.5モル%のエチレン―
プロピレンランダム共重合体70重量%と、酢酸ビ
ニル含有量15重量%のエチレン―酢酸ビニル共重
合体30重量%からなる厚さ100μの熱可塑性フイ
ルムを押出し、前記の発泡シート上に直接溶融押
出しラミネートしたところ、両者は熱可塑性フイ
ルム押出時の残熱によりかなり接着されていた。
しかる後表面温度100〜110℃を有する等速の予熱
ロール3連により充分予熱し、次いで速度比1:
5表面温度45℃の延伸ロールを通して縦方向に5
倍に延伸し、更に延伸ロールと同速で表面温度30
℃の冷却ロールを通すことにより発泡層180μ、
ラミネート層20μを有する厚さ200μの複合発泡フ
イルムを得た。このフイルムの発泡層とラミネー
ト層は延伸工程で強力に接着しており、縦方向に
熱収縮する好ましいものであつた。
〈実施例 2〉
弾性改質用重合体としてエチレン含有量92モル
%、密度0.90g/cm3、結晶化度10%のエチレン―
1―ブテンランダム共重合体を用い、かつラミネ
ート層の熱可塑性フイルムとしてエチレン含有量
4.5モル%のエチレン―プロピレンランダム共重
合体70重量%とエチレン含有量92モル%密度0.90
g/cm3、結晶化度10%のエチレン―1―ブテンラ
ンダム共重合体30重量%の配合物を用いる以外、
実施例1と同様にして同様の複合発泡材料(フイ
ルム)を得た。
〈実施例 3〉
発泡剤として重炭酸ナトリウムとクエン酸を使
用(使用量20重量%)した主成分が低密度ポリエ
チレンのマスターペレツト5重量部(発泡剤成分
は1重量部)を用いる以外実施例1と同様の組成
物を用い、同様に製膜して厚さ900μのフラツト
状発泡シートを得た。しかる後、実施例1と同様
にラミネート層を形成した後、実施例1と同様に
ロール延伸を行い、縦方向に約5倍に延伸したと
ころ、発泡層180μ、ラミネート層20μの合計厚さ
200μである縦方向に熱収縮する複合発泡フイル
ムを得た。
〈比較例 1〉
エチレン含有量4.5モル%のエチレン―プロピ
レンランダム共重合体100重量部に重炭酸ナトリ
ウムとクエン酸とからなる発泡剤1重量部を加え
た配合組成物を実施例1と同様にして厚さ900μ
の発泡フイルムを得、前記共重合体単品からなる
厚さ100μの熱可塑性フイルムを溶融押出しラミ
ネートによりラミネートした。次いでテンターに
より実施例1と同様に縦延伸したところ、この複
合発泡材料(フイルム)は発泡層の面のセルがと
ころどころ破裂しており表面が毛羽立つていた。
〈比較例 2〉
ポリスチレンに比較例1と同様の発泡剤を同量
加え、同様に製膜して厚さ510μの発泡シートを
得た。一方ポリスチレンのみからなる厚さ90μの
フイルムを押出し、溶融押出しラミネート法によ
り前記発泡シートにラミネートして、しかる後、
110℃の温度で3倍にロール延伸を行なつたとこ
ろ、厚さ200μの縦方向に熱収縮する複合フイル
ムを得た。
以上の実施例1,2,3と比較例2で得られた
複合発泡フイルムの各物性を下記第1表に掲げ
る。
The present invention relates to a composite foam material having excellent cushioning effect, printability, etc. and having heat shrinkability in the longitudinal direction. Conventionally, heat-shrinkable foam materials such as foam sheets and films have mainly been made from polystyrene, which has been particularly effective in preventing bottles from breaking when used for the exterior of containers such as bottles. It is well known as a useful packaging material because it exhibits a cushioning effect. However, heat-shrinkable foam sheets or films made of polystyrene are weak and fragile due to the characteristics of their raw materials, and are not used for labels that have the effect of preventing bottles from breaking or having a cushioning effect. However, the disadvantage is that the foamed material is damaged during the cleaning process, filling process, and even transportation, and even if the surface of the material is printed, it cannot be clearly printed, and the foamed material is layered. Phenomena such as curling and partial peeling were observed, which was a problem. This invention was made in order to solve the above-mentioned problems, and as a composite foam material having heat shrinkability in the longitudinal direction, an ethylene-propylene copolymer having an ethylene content of 1 to 10 mol%, A composition containing an elasticity-modifying polymer and a foaming agent is formed into a film, and then stretched in the longitudinal direction to form a foam material having heat-shrinkability in the longitudinal direction. The gist of the invention is that thermoplastic films are laminated, and the invention will be described in detail below. The ethylene-propylene copolymer used in the present invention usually has an ethylene content of 1 to 10 mol%, preferably 2 to 6 mol%; if the ethylene content exceeds 10 mol%, the produced foam material becomes sticky. If it is less than 1 mol %, its properties are too close to those of polypropylene, and therefore the shrinkage rate is small even when stretched, making it unsatisfactory as a heat-shrinkable member and causing the foam cells to tear. The phenomenon of fluffing becomes more likely. Preferably, the copolymer contains ethylene randomly. At this time, the amount of the copolymer to be used may be an appropriate amount that exhibits the effect, but it is preferably about 50 to 95% by weight based on the total amount of the polymer. Next, the elasticity-modifying polymer used in the present invention is added to give elasticity to the foam cells of the foam material, and if this polymer is not added, it will not be able to withstand the internal pressure during foaming. First, the foam cells tend to expand, making it impossible to obtain a fine foam structure. This polymer preferably has the property of imparting elasticity to cells during foaming; examples include low, medium,
Contains polar groups such as high-density polyethylene, polybutene, ethylene-vinyl acetate copolymer, ethylene-ethyl acrylate, ethylene-1-butene copolymer, propylene-1-butene copolymer, unsaturated carboxylic acid and its derivatives, etc. Typical examples include modified polyolefin, 1:2 type polybutadiene, and linear low density polyethylene (LL DPE). In this case, a more preferable elasticity-modifying polymer is ethylene-vinyl acetate containing 3 to 40% by weight.
Examples include vinyl acetate copolymers and ethylene-1-butene random copolymers having an ethylene content of 85 to 95 mol% (density 0.86 to 0.91, crystallinity 3 to 20%). The amount of the elasticity-modifying polymer to be used may be at least an amount that exhibits its effect, and preferably about 5 to 50% by weight based on the total amount of the polymer. The blowing agent used in the present invention may be any known blowing agent. Examples of suitable blowing agents include pentane and butane as volatile ones, and hydrazine as organic ones. There are nitroso-based, nitroso-based, azo-based, etc., and inorganic ones such as sodium bicarbonate and ammonia carbonate. In this case, more preferable examples include azo blowing agents such as azodicarbonamide and azobisisobutyronitrile, and inorganic blowing agents including carbonates such as sodium bicarbonate and ammonium carbonate, and citric acid.
Examples include those consisting of an organic acid such as acetic acid. The amount of this blowing agent to be used should be at least the amount that exhibits its effect, but the total amount of the ethylene-propylene copolymer with an ethylene content of 1 to 10 mol% and the elasticity-modifying polymer ( The total amount of polymer may be 0.2 to 5 parts by weight, more preferably 0.5 to 2 parts by weight, based on 100 parts by weight. The above blowing agent may be directly blended with the ethylene-propylene copolymer according to the present invention, or may be blended with the addition of master pellets containing a high concentration of blowing agent.
An appropriate amount of a blowing agent may be kneaded into the copolymer in advance, and there are no particular restrictions on its usage. In addition, in the present invention, appropriate additives, fillers, etc. may be added in addition to the above three components, and for example, lubricants, antistatic agents, etc. may be added as necessary to improve physical properties. If necessary, desired coloring can be achieved by adding a pigment. Next, in the present invention, in order to improve the printability of the foamed material and improve its surface condition, a laminate layer is formed on the foamed material. Examples of the plastic film include films made of various commonly used thermoplastic polymers, and are not particularly limited. Examples of polyolefin resins include low, medium, and high density polyethylene, polypropylene and its copolymers, polyamide resins, polyester resins, polyvinyl resins, ethylene-vinyl acetate copolymers, and ethylene. -1-butene copolymer, etc. Among these, particularly preferred examples are those made of the same kind of polymer as the foamed material of the present invention, such as an ethylene-propylene copolymer with an ethylene content of 1 to 10 mol% or, for example, a vinyl acetate content of 3 to 40% by weight. For elastic modification of ethylene-vinyl acetate copolymers, ethylene-1-butene random copolymers with an ethylene content of 85 to 95 mol%, a density of 0.86 to 0.91 g/cm 3 , and a crystallinity of 3 to 20%. When a polymer is used alone or as a blend thereof, an anchor coat layer is not required and it is possible to directly laminate with the foam material by thermocompression bonding, which is extremely convenient. On the other hand, if a different type of thermoplastic film is used, it may be difficult to collect and reuse the scraps, but of course it can be used. Note that the thermoplastic film forming the laminate layer may also contain appropriate additives and fillers, such as lubricants,
If necessary, an antistatic agent or the like may be added to improve the physical properties, and if necessary, a pigment can be added to provide the desired coloration. The composite foamed material according to the present invention can be exemplified by laminating a thermoplastic film on a foamed material such as a film or sheet-like material, and the shape is not particularly limited, but a film or sheet-like material may be stretched. This is a suitable example because it is easy to operate. In the present invention, a composition for foamed materials or thermoplastic films containing the above-mentioned components is formed into a film, and then stretched in the longitudinal direction. The purpose of stretching in the longitudinal direction is to impart heat shrinkability in the longitudinal direction, and this is achieved by stretching in the direction in which the foamed material is produced, that is, in the longitudinal direction. Further, in the present invention, the most preferable results can be obtained if the flat foam material is longitudinally stretched by so-called roll stretching, in which the flat foam material is passed between rolls having different speeds. At this time, as a specific example of roll stretching, a method is exemplified in which the rolls are preheated to a temperature that allows stretching through several uniform speed preheating rolls, and then stretched to a desired magnification by stretching rolls set at a predetermined stretching ratio. can. The preheating roll temperature may be set as appropriate, but preferably
It is recommended to set the temperature between 90 and 130℃. If the temperature is too high, the low-temperature shrinkability will be impaired, requiring high temperatures during shrinkage, resulting in energy loss and the problem of partial melting of the sheet, while if it is too low, large stresses will occur during stretching. However, it is possible to implement this method, although it is not preferable since the mechanical load may increase or tearing may occur. The above-mentioned stretching rolls may be used as appropriate, but they are generally set at a temperature lower than that of the preheating rolls, for example, 60°C or less, and the sheet stretched here is gradually lowered by several cooling rolls so that natural shrinkage does not occur at room temperature. One way is to make it less likely to happen. The above explanation has been made using a flat film as an example, but a tubular film is difficult to combine, but it is possible to implement it. At this time, if longitudinal stretching is carried out using a normal inflation method, it is conceivable that some orientation may occur in the transverse direction, but these are all within the scope of the present invention, and the same applies to flat-shaped materials. Other longitudinal stretching means are not limited to those described above. Next, as an example of creating the composite foam material of the present invention, the method of forming a film or sheet using an extruder, then melt extrusion laminating a thermoplastic film, forming a laminate layer, and then longitudinally stretching is described below. state First, the conditions of the extruder were set to such an extent that a composition containing an ethylene-propylene copolymer with an ethylene content of 1 to 10 mol%, an elasticity-modifying polymer, and a foaming agent would not foam in the die. It can be extruded from a die into a flat sheet. At this time, it is preferable to foam at the same time. On the other hand, 1 to 10 ethylene of the same type as the raw material composition of the foamed material
At the same time, extruding a thermoplastic resin compound consisting of mol% of ethylene-propylene copolymer and an elasticity modifying polymer, melt extrusion and lamination onto the foamed material (foamed sheet), and laminated with a thermoplastic film. form a layer. At this time, the thermoplastic film is easily laminated and integrated with the foam sheet using a simple nip roll due to the heat generated during extrusion. Next, the foamed sheet and the thermoplastic film are stretched in the longitudinal direction by roll stretching, and as a result of this stretching, the foamed sheet and the thermoplastic film are bonded more strongly, and the two become as if they were a single layer, making it extremely difficult to separate them. Next, the stretching temperature (including preheating temperature)
However, this can be selected as appropriate, but for example 90~
130°C is preferred. In addition, the stretching ratio should be selected as necessary, but it should be at least 2 times, or 3 times if necessary.
It is only necessary to stretch the material by a factor of about 8 to 8. If the stretching is carried out under the above-mentioned numerical conditions, a composite foam material having preferable heat shrinkability in the longitudinal direction can be obtained, but the present invention is of course not limited to this. In this way, a composite foam material is created. At this time, the thickness of the foam material and thermoplastic film can be selected appropriately depending on the application, and in order to improve printability, the surface of the thermoplastic film can be It is also free to apply surface treatment such as corona discharge treatment. The above is a method of laminating the same type of thermoplastic film on a foam material (foamed sheet) by melt extrusion.
Simultaneously with foaming, the film may be laminated by pressing it onto a foamed sheet using a nip roll or the like. At this time, since the heat from extrusion remains on the foam sheet side, the two can be laminated and integrated extremely easily. Further, it is preferable that the foaming be carried out at the same time as the film formation, but it goes without saying that the foaming may be carried out before the film formation, after the film formation, or even simultaneously with the stretching. The above is just a description of the preferred method for manufacturing the composite foam material according to the present invention, and the present invention can also employ other appropriate methods. The composite foam material according to the present invention is most often used as a printed exterior heat-shrinkable foam label for bottles, etc., and is used in a cylindrical shape so that the stretching direction coincides with the circumferential direction of the bottle, etc. It is also widely used as a packaging material for various containers and articles, and its range of applications is wide and there are no particular limitations. Considering these uses, it is most preferable to use the composite foam material in the form of a sheet or film. The present invention is as described above, and when the composite foam material according to the present invention is used, for example, as an exterior label for a bottle or the like, it is particularly excellent in bottle breakage prevention effect and cushioning effect. It also has excellent physical properties such as strength and is not brittle like conventional products, so it can be folded into a cylindrical body, for example, and the creases that occur when folding are removed during heat shrinkage. Not only does it have the property of disappearing, but it also has remarkable effects such as being strong and strong without the disadvantage that it easily peels off in layers from the edges of the material. Examples of the present invention will be listed below along with comparative examples. <Example 1> 70% by weight of an ethylene-propylene random copolymer with an ethylene content of 4.5 mol% and 30% by weight of an ethylene-vinyl acetate copolymer (elasticity modification polymer) with a vinyl acetate content of 15% by weight 1 part by weight of a blowing agent consisting of a mixture of sodium bicarbonate and citric acid was mixed with 100 parts by weight of the mixture, and the mixture was extruded and foamed into a flat sheet through a die of an extrusion molding machine to create a foam sheet with a thickness of 900μ. . On the other hand, ethylene with an ethylene content of 4.5 mol%
A 100μ thick thermoplastic film consisting of 70% by weight propylene random copolymer and 30% by weight ethylene-vinyl acetate copolymer with 15% vinyl acetate content was extruded and laminated directly onto the foam sheet by melt extrusion. As a result, it was found that the two were considerably bonded together due to residual heat from extrusion of the thermoplastic film.
After that, it was sufficiently preheated using three sets of uniform speed preheating rolls having a surface temperature of 100 to 110°C, and then the speed ratio was 1:
5 in the longitudinal direction through a stretching roll with a surface temperature of 45°C.
Stretched twice, then at the same speed as the stretching roll at a surface temperature of 30
Foam layer 180μ by passing through a cooling roll at ℃
A composite foamed film with a thickness of 200μ with a laminate layer of 20μ was obtained. The foamed layer and laminate layer of this film were strongly bonded during the stretching process, and the film was preferably thermally shrinkable in the longitudinal direction. <Example 2> Ethylene with an ethylene content of 92 mol%, a density of 0.90 g/cm 3 , and a crystallinity of 10% as an elasticity-modifying polymer
Using 1-butene random copolymer and ethylene content as a thermoplastic film of the laminate layer.
4.5 mol% ethylene-propylene random copolymer 70% by weight and ethylene content 92 mol% density 0.90
g/cm 3 , except using a formulation of 30% by weight of ethylene-1-butene random copolymer with 10% crystallinity.
A similar composite foam material (film) was obtained in the same manner as in Example 1. <Example 3> Except for using 5 parts by weight of master pellets whose main component is low-density polyethylene (the blowing agent component is 1 part by weight) using sodium bicarbonate and citric acid as blowing agents (amount used: 20% by weight) Using the same composition as in Example 1, a film was formed in the same manner as in Example 1 to obtain a flat foam sheet with a thickness of 900 μm. After that, a laminate layer was formed in the same manner as in Example 1, and then roll stretching was carried out in the same manner as in Example 1, and when it was stretched approximately 5 times in the longitudinal direction, the total thickness of the foam layer was 180 μm and the laminate layer was 20 μm.
A longitudinally heat-shrinkable composite foam film having a thickness of 200μ was obtained. <Comparative Example 1> A blended composition in which 1 part by weight of a blowing agent consisting of sodium bicarbonate and citric acid was added to 100 parts by weight of an ethylene-propylene random copolymer with an ethylene content of 4.5 mol% was prepared in the same manner as in Example 1. thickness 900μ
A foamed film was obtained, and a thermoplastic film having a thickness of 100 μm made of the single copolymer was laminated by melt extrusion lamination. When the composite foam material (film) was then longitudinally stretched using a tenter in the same manner as in Example 1, the cells on the surface of the foam layer were ruptured in places and the surface was fluffy. <Comparative Example 2> The same amount of the same foaming agent as in Comparative Example 1 was added to polystyrene, and a film was formed in the same manner to obtain a foamed sheet with a thickness of 510 μm. On the other hand, a 90μ thick film made only of polystyrene was extruded and laminated on the foam sheet by melt extrusion lamination method, and then,
Roll stretching was carried out three times at a temperature of 110°C to obtain a longitudinally heat-shrinkable composite film with a thickness of 200 μm. The physical properties of the composite foamed films obtained in Examples 1, 2, and 3 and Comparative Example 2 are listed in Table 1 below.
【表】
上記の第1表から本発明の実施例1,2,3の
各複合発泡材料は強靭で、引裂強度に優れ、衝撃
強度が抜群で、伸度も適度に備わつた極めて実用
的な熱収縮性材料であることが立証された。これ
に対し比較例1のものは満足な材料とならなかつ
たし、比較例2のものも衝撃強度その他諸物性が
極めて悪く、緩衝効果がもう一つ不充分である上
に、例えばラミネート層が取扱中や洗浄中に剥離
する等の現象もみられ、また両層とも剥げ落ちる
等の現象も見られた。このことからも本発明の格
別顕著な効果がうかゞえる。[Table] From Table 1 above, the composite foam materials of Examples 1, 2, and 3 of the present invention are tough, have excellent tear strength, excellent impact strength, and have moderate elongation, making them extremely practical. It has been proven that it is a heat-shrinkable material. On the other hand, the material of Comparative Example 1 was not a satisfactory material, and the material of Comparative Example 2 also had extremely poor impact strength and other physical properties, and the buffering effect was insufficient. Phenomena such as peeling during handling and washing were also observed, and phenomena such as both layers peeling off were also observed. This also shows that the present invention has particularly significant effects.
Claims (1)
プロピレン共重合体と、弾性改質用重合体、及び
発泡剤とを配合した組成物を製膜し、しかる後縦
方向に延伸されることにより縦方向に熱収縮性を
有する発泡材料に、縦方向に熱収縮性を有する熱
可塑性フイルムがラミネートされてなることを特
徴とする、縦方向に熱収縮性を有する複合発泡材
料。1 Ethylene with an ethylene content of 1 to 10 mol%
A composition containing a propylene copolymer, an elasticity-modifying polymer, and a foaming agent is formed into a film, and then stretched in the longitudinal direction to form a foamed material having heat shrinkability in the longitudinal direction. A composite foam material that is heat-shrinkable in the longitudinal direction and is characterized by being laminated with a thermoplastic film that is heat-shrinkable in the longitudinal direction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57161284A JPS5949958A (en) | 1982-09-16 | 1982-09-16 | Composite foamed material having heat shrinkage in transverse direction |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57161284A JPS5949958A (en) | 1982-09-16 | 1982-09-16 | Composite foamed material having heat shrinkage in transverse direction |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5949958A JPS5949958A (en) | 1984-03-22 |
| JPH0153184B2 true JPH0153184B2 (en) | 1989-11-13 |
Family
ID=15732177
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57161284A Granted JPS5949958A (en) | 1982-09-16 | 1982-09-16 | Composite foamed material having heat shrinkage in transverse direction |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5949958A (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2893286B2 (en) * | 1990-05-17 | 1999-05-17 | グンゼ株式会社 | Heat-shrinkable foamed composite film and method for producing the same |
| US5851610A (en) * | 1991-02-07 | 1998-12-22 | Applied Extrusion Technologies, Inc. | Shrink films and articles including the same |
| US5460878A (en) * | 1992-10-26 | 1995-10-24 | Applied Extrusion Technologies, Inc. | Heat sealable shrink laminate |
| IT1312057B1 (en) * | 1999-04-09 | 2002-04-04 | Bimo Italia S P A | Shrinkable plastic films. |
| WO2015004314A1 (en) * | 2013-07-12 | 2015-01-15 | Upm Raflatac Oy | Multilayer film for label and a method for providing such |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5845976B2 (en) * | 1976-04-30 | 1983-10-13 | 三井化学株式会社 | Polypropylene film for shrink wrapping |
| JPS5540413A (en) * | 1978-09-15 | 1980-03-21 | Olympus Optical Co Ltd | Test light emitting device of ttl control strobe |
| US4244900A (en) * | 1979-03-26 | 1981-01-13 | Owens-Illinois, Inc. | Method for the continuous production of a co-extruded heat-shrinkable composite foamed resin sheet |
-
1982
- 1982-09-16 JP JP57161284A patent/JPS5949958A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5949958A (en) | 1984-03-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP2958363B2 (en) | Stretch / shrink film with improved oxygen permeability | |
| US4469752A (en) | Cold drawn high-orientation multilayered film and process for manufacture of said film | |
| US4835218A (en) | Composition for drawn film, cold film made of said composition and process for manufacture of said film | |
| US20020029844A1 (en) | Labels | |
| JPS63264349A (en) | Flexible expansion film | |
| US6699418B2 (en) | Method for producing biaxially stretched film made of ethylene-vinyl alcohol copolymer | |
| JPH0470987B2 (en) | ||
| JP2893286B2 (en) | Heat-shrinkable foamed composite film and method for producing the same | |
| JPS6150974B2 (en) | ||
| US20090017297A1 (en) | In-mold label with foamed adhesive skin | |
| JPH0153184B2 (en) | ||
| JP3071244B2 (en) | High transparency and high gloss oriented film | |
| JP2001219522A (en) | Polylactic acid-based laminated biaxially stretched film | |
| JPS6222787B2 (en) | ||
| JPH0138662B2 (en) | ||
| JP2008105428A (en) | Polylactic acid-based laminated biaxially stretched film | |
| JPH0138663B2 (en) | ||
| JPH0428737B2 (en) | ||
| JPS5925825A (en) | Expanded material having heat sherinkability in crosswise direction | |
| JPH0339827B2 (en) | ||
| JP2821252B2 (en) | Sealant film | |
| CA2207698C (en) | Multilayered polyolefin high shrinkage, low shrink force shrink film | |
| JPS6044139B2 (en) | insulating packaging material | |
| JPH0341347B2 (en) | ||
| JP2006289986A (en) | Polylactic acid-based laminated biaxially stretched film |