JPH0550378B2 - - Google Patents
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- Publication number
- JPH0550378B2 JPH0550378B2 JP24268185A JP24268185A JPH0550378B2 JP H0550378 B2 JPH0550378 B2 JP H0550378B2 JP 24268185 A JP24268185 A JP 24268185A JP 24268185 A JP24268185 A JP 24268185A JP H0550378 B2 JPH0550378 B2 JP H0550378B2
- Authority
- JP
- Japan
- Prior art keywords
- film
- stretching
- sheet
- weight
- minutes
- 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
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- Manufacture Of Macromolecular Shaped Articles (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Description
〔産業上の利用分野〕
本発明はラベル用の熱収縮フイルムの製造方法
に関するものであり、更に詳しくは耐熱性に優れ
るポリオレフイン系の熱収縮フイルムの製造方法
である。
〔従来の技術〕
従来、ワンウエイ用容器、特にガラス瓶のラベ
ルとして使用されている熱収縮フイルムの素材に
は、ポリ塩化ビニル樹脂やポリスチレン系樹脂が
あるが、これらの素材は耐熱性に劣り、100℃を
越す高温殺菌工程を必要とする内容物(例えばコ
ーヒー飲料)用ラベルとしては使用できない。一
方、本発明者らは、ポリオレフイン系の発泡シー
トが緩衝性、耐衝撃強度、耐熱性等の利点より優
れたラベル用熱収縮フイルムであることを開示し
た(特願昭60−4926号)。
しかしながら、発泡シートは不透明である為ガ
ラス瓶に被覆する場合、被覆する高さに制限のあ
ることや、ソリツドフイルムに比べた場合、熱伝
導度が小さく、内容物を所定の温度まで加熱する
工程や冷却する工程をもつ充填ラインではライン
速度を下げざるを得えない欠点を有している。
〔問題を解決する為の手段〕
本発明者らは、この様な状況下に耐熱性及び透
明性の優れるしかもフイルムの装着する機械適性
の良い熱収縮フイルムを鋭意検討した結果、特定
のエチレン−プロピレン共重合体を使つた一方方
向延伸フイルムが有効であることを見い出し、本
発明を完成するに至つた。
すなわち本発明は、エチレン含有量が2〜10重
量%であつて、メルトフローインデツクス
(MI;LISK−6758に準ずる)が0.5〜10g/10分
であるエチレン−プロピレン共重合体100重量と、
メルトフロ−インデツクスが0.5〜10g/10分で
あるプロピレン単独重合体0〜50重量部からなる
組成物よりシートを成形し、該シート表裏の表面
温度差を2℃以上もたせて一方方向に延伸するこ
とを特徴とするオレフイン系収縮フイルムの製造
方法である。
以下、本発明を詳細に説明する。
本発明でいうエチレン−プロピレンの共重合体
は、エチレンの含有量が2〜10重量%好ましくは
3〜7重量%のものである。エチレンの含有量が
2重量%未満では延伸したフイルムの収縮温度巾
が狭く、熱風をフイルムに吹き付けた際、直接熱
風が当ると溶融状態になり、また熱風の当たりが
弱いと収縮不足になり、被覆したガラス瓶全周を
奇麗にすることが困難でロスが大きい。又、エチ
レン含有量が10重量%を越えると剛性が低下し、
フイルムをガラス瓶に装着する際ロスが多発した
り、耐熱性が低下してくる。
エチレン−プロピレン共重合体100重量に対し
て、プロピレン単独重合体を0〜50重量部の範囲
で耐熱性、加熱時の収縮性、剛性等の必要物性に
応じ選択配合される。プロピレン単独重合体の配
合量が50重量部を越えると延伸フイルムの収縮温
度巾が狭くなり、ガラス瓶に被覆時の外観不良の
ロスが多発する。
エチレン−プロピレン共重合体のメルトインデ
ツクス(MI;JISK−6758に準ずる)は、0.5〜10
g/10分、好ましく1.0〜5g/10分の範囲であ
る。プロピレン単独重合体のMI値は0.5〜10g/
10分で好ましくはエチレン−プロピレン共重合体
のMI値±1g/10分である。MI値が0.5g/10
分未満ではフイルムの延伸ムラを発生したりフイ
ルム裂けを発生する。また逆に10g/10分を越す
と延伸をかけてその効果が乏しく、特に加熱時の
収縮が不足しロスが大きくなる。
本発明において着色剤、帯防剤、酸化防止剤等
を添加することは何ら差し支えない。
本発明の熱収縮フイルムを得る為の延伸処理は
縦方向もしくは横方向に少なくとも一方方向に延
伸するものであつて、好ましくは縦方向に延伸す
る。
縦方向に延伸する際は通常ロール延伸機が使用
され、予熱は100〜140℃の温度範囲で行われ、か
つシートの表裏の表面温度差が2℃以上で引取方
向に延伸される。延伸倍率は3.0〜7.0倍、好まし
くは4.0〜6.0倍が選択される。
予熱温度が100℃未満では、延伸ムラが発生し
易く均一な収縮フイルムを得ことが困難になり、
又140℃を越えると延伸効果が損われる。又シー
ト表裏の表面温度差が2℃未満では、延伸したフ
イルムからラベル用としてヒートシールして円筒
体を作成した後、加熱炉に挿入した際、円筒体の
内面を強く収縮せしめ内側に巻き込む状態で収縮
することができず、収縮時に折れジワが多発し、
奇麗な被覆瓶が得られない。
延伸倍率は3.0倍未満では収縮性が不足し、こ
の為装着したラベルを加熱した際ガラス瓶に密着
せず肩部にシワが多発する。又逆に、7.0倍を越
えると延伸方向に裂け易くスリツト等の工程で支
障をきたす。
横方向に延伸する際は、テンター方式が代表的
手段として用いられ、予熱条件および延伸倍率は
縦方向の延伸と同様の条件が適用される。
〔実施例〕
以下、実施例にて本発明を説明する。
実施例 1〜2
表に示した樹脂を原料として50mmφ押出機に取
付た300mm巾のTダイよりシートを押出し、この
シートを表に示した延伸条件で80μmの厚みのフ
イルムを得た。
このフイルムの収縮率及び実用テストの実施し
た結果を表に記載した。
収縮率の測定条件;120℃の油浴中1分間浸漬
耐熱ブロツキング性の測定条件;被覆ビンを3本
1組に縛り110℃の乾燥機中に20分間放置。
加熱時の収縮性能もあり、ガラス瓶にフイルム
円筒体を被せて加熱収縮させた後の外観も良好で
あつた。110℃の乾燥機中に放置してもフイルム
は変形せず、耐熱性に優れている。
又、実施例1のフイルムを被覆(ラベルの高さ
105mm)した瓶(内容量312c.c.)と、ポリオレフイ
ン発泡シート(シート厚0.2mm、発泡倍率1.5倍、
ラベル高さ105mm)を被覆した瓶を用意し、25℃
の水300c.c.充填した後、90℃の恒温水槽中に105mm
浸漬し、ガラス瓶内の水温の変化をフイルムを被
覆した瓶内水温がポリオレフイン発泡シートを被
覆した瓶内水温と同一に達する所要時間は約半分
であつた。
比較例 1−3
実施例1と同様の設備および原料を使用し、延
伸条件を表に示した如くに変えてフイルムを得
た。比較例1のフイルムは、厚みバラツキも大で
製品ロスが大きかつた。又比較例2、3のフイル
ムはいずれもガラス瓶にフイルムを被せて加熱さ
せた際、奇麗に収縮せずロスが多かつた。
比較例 4
原料としてスチレン−ブタジエン共重合体を使
用し、5倍延伸して80μmのフイルムを得た。こ
のフイルムをガラス瓶に被覆し、3本を1組に縛
り、110℃の温度の乾燥後に20分間放置した。ブ
ロツキングし、又フイルムも変形してしまつた。
[Industrial Application Field] The present invention relates to a method for producing a heat-shrinkable film for labels, and more specifically to a method for producing a polyolefin-based heat-shrinkable film having excellent heat resistance. [Prior art] Conventionally, heat-shrinkable film materials used as labels for one-way containers, especially glass bottles, include polyvinyl chloride resin and polystyrene resin, but these materials have poor heat resistance and It cannot be used as a label for contents (such as coffee drinks) that require a high temperature sterilization process exceeding ℃. On the other hand, the present inventors have disclosed that a polyolefin foam sheet is a heat-shrinkable film for labels that has superior advantages such as cushioning properties, impact strength, and heat resistance (Japanese Patent Application No. 4926/1983). However, since foam sheets are opaque, there is a limit to the height of the coating when covering glass bottles, and when compared to solid films, the thermal conductivity is low, and the process of heating the contents to a predetermined temperature is difficult. A filling line with a cooling process has the disadvantage that the line speed must be reduced. [Means for Solving the Problem] Under these circumstances, the inventors of the present invention have intensively studied a heat-shrinkable film that has excellent heat resistance and transparency, and has good mechanical suitability for mounting the film. It was discovered that a unidirectionally stretched film using a propylene copolymer is effective, and the present invention was completed. That is, the present invention provides 100 weight ethylene-propylene copolymers having an ethylene content of 2 to 10% by weight and a melt flow index (MI; according to LISK-6758) of 0.5 to 10 g/10 minutes;
Forming a sheet from a composition consisting of 0 to 50 parts by weight of a propylene homopolymer having a melt flow index of 0.5 to 10 g/10 minutes, and stretching in one direction with a surface temperature difference of 2°C or more between the front and back surfaces of the sheet. This is a method for producing an olefin-based shrink film characterized by the following. The present invention will be explained in detail below. The ethylene-propylene copolymer used in the present invention has an ethylene content of 2 to 10% by weight, preferably 3 to 7% by weight. If the ethylene content is less than 2% by weight, the stretched film will have a narrow shrinkage temperature range, and when hot air is blown onto the film, it will become molten if the hot air hits it directly, and if the hot air hits it weakly, it will not shrink enough. It is difficult to clean the entire circumference of the coated glass bottle, resulting in large losses. In addition, when the ethylene content exceeds 10% by weight, the rigidity decreases,
When attaching the film to a glass bottle, there is a lot of loss and the heat resistance decreases. Based on 100 weight parts of the ethylene-propylene copolymer, 0 to 50 parts by weight of the propylene homopolymer is selected and blended in accordance with required physical properties such as heat resistance, shrinkability upon heating, and rigidity. If the amount of propylene homopolymer blended exceeds 50 parts by weight, the shrinkage temperature range of the stretched film becomes narrow, resulting in frequent losses due to poor appearance when coating glass bottles. The melt index (MI; according to JISK-6758) of ethylene-propylene copolymer is 0.5 to 10.
g/10 minutes, preferably in the range of 1.0 to 5 g/10 minutes. The MI value of propylene homopolymer is 0.5-10g/
In 10 minutes, the MI value of the ethylene-propylene copolymer is preferably ±1 g/10 minutes. MI value is 0.5g/10
If it is less than 1 minute, uneven stretching or tearing of the film may occur. On the other hand, if it exceeds 10 g/10 minutes, the effect of stretching will be poor, especially shrinkage during heating will be insufficient and loss will increase. In the present invention, there is no problem in adding colorants, anti-static agents, antioxidants, etc. The stretching treatment for obtaining the heat-shrinkable film of the present invention involves stretching in at least one direction, either the machine direction or the transverse direction, preferably in the machine direction. When stretching in the machine direction, a roll stretching machine is usually used, preheating is performed at a temperature in the range of 100 to 140°C, and the sheet is stretched in the take-off direction at a temperature difference of 2°C or more between the front and back surfaces of the sheet. The stretching ratio is selected to be 3.0 to 7.0 times, preferably 4.0 to 6.0 times. If the preheating temperature is less than 100℃, uneven stretching will easily occur and it will be difficult to obtain a uniform shrink film.
Moreover, if the temperature exceeds 140°C, the stretching effect will be impaired. In addition, if the surface temperature difference between the front and back of the sheet is less than 2°C, when a cylindrical body is made from a stretched film by heat sealing for labels and then inserted into a heating furnace, the inner surface of the cylindrical body will contract strongly and become rolled inward. It cannot be contracted, and many folds and wrinkles occur during contraction.
A beautiful coated bottle cannot be obtained. If the stretching ratio is less than 3.0 times, the shrinkability will be insufficient, and for this reason, when the attached label is heated, it will not adhere tightly to the glass bottle and wrinkles will occur frequently on the shoulder. On the other hand, if it exceeds 7.0 times, it tends to tear in the stretching direction, causing problems in slitting and other processes. When stretching in the transverse direction, a tenter system is typically used, and the same preheating conditions and stretching ratio as in the longitudinal stretching are applied. [Example] The present invention will be described below with reference to Examples. Examples 1-2 A sheet was extruded from a 300 mm wide T-die attached to a 50 mmφ extruder using the resin shown in the table as a raw material, and a film with a thickness of 80 μm was obtained by stretching this sheet under the stretching conditions shown in the table. The shrinkage rate of this film and the results of practical tests are listed in the table. Conditions for measuring shrinkage: Immersion in an oil bath at 120°C for 1 minute. Conditions for measuring heat-resistant blocking properties: Tie the coated bottles into a set of 3 and leave in a dryer at 110°C for 20 minutes. It also had good shrinkage performance when heated, and had a good appearance after the glass bottle was covered with a film cylinder and heat-shrinked. The film does not deform even if left in a dryer at 110℃, and has excellent heat resistance. In addition, the film of Example 1 was coated (the height of the label
105 mm) bottle (inner capacity 312 c.c.) and a polyolefin foam sheet (sheet thickness 0.2 mm, foaming ratio 1.5 times,
Prepare a bottle coated with a label (label height 105 mm) and heat it at 25℃.
After filling 300c.c. of water, 105mm in a constant temperature water tank at 90℃
The time required for the water temperature in the glass bottle covered with the film to reach the same temperature as the water temperature in the bottle covered with the polyolefin foam sheet was about half the time required for immersion in the glass bottle. Comparative Example 1-3 A film was obtained using the same equipment and raw materials as in Example 1, but changing the stretching conditions as shown in the table. The film of Comparative Example 1 had large variations in thickness, resulting in large product loss. Furthermore, when the films of Comparative Examples 2 and 3 were placed on a glass bottle and heated, they did not shrink neatly and there was a lot of loss. Comparative Example 4 A styrene-butadiene copolymer was used as a raw material and stretched 5 times to obtain a film of 80 μm. This film was coated on a glass bottle, three bottles were tied into a set, and after drying at a temperature of 110°C, the bottles were left for 20 minutes. There was blocking and the film was also deformed.
本発明で得られた熱収縮フイルムは耐熱性に優
れ、100℃を越える加熱殺菌工程を通過する容器
のラベルとしても使用が可能であり、ガラス瓶は
もとよりPET樹脂ボトルや金属缶等のラベルと
してもて適用できる。
さらに本発明で得られたフイルムは透明性にも
優れ、耐衝撃性もあるので内圧のかかつている炭
素飲料用ガラス瓶の被覆ラベルとしても充分使用
可能である。
The heat-shrinkable film obtained by the present invention has excellent heat resistance and can be used as a label for containers that undergo a heat sterilization process at temperatures exceeding 100°C, as well as labels for glass bottles, PET resin bottles, metal cans, etc. can be applied. Furthermore, the film obtained by the present invention has excellent transparency and impact resistance, so it can be used satisfactorily as a cover label for glass bottles for carbon beverages which are subjected to internal pressure.
Claims (1)
ルトフローインデツクス(MI;JIS K−6758)
が0.5〜10g/10分であるエチレン−プロピレン
共重合体100重量部とメルトフローインデツクス
が0.5〜10g/10分であるプロピレン単独重合体
0〜50重量部からなる組成物よりシートを成形
し、該シートを100〜140℃の温度で予熱しかつシ
ート表裏の表面温度差を2℃以上もたせて一方方
向に延伸することを特徴とするオレフイン系収縮
フイルムの製造方法。1 Ethylene content is 2 to 10% by weight, and melt flow index (MI; JIS K-6758)
A sheet is formed from a composition consisting of 100 parts by weight of an ethylene-propylene copolymer having a melt flow index of 0.5 to 10 g/10 minutes and 0 to 50 parts by weight of a propylene homopolymer having a melt flow index of 0.5 to 10 g/10 minutes. . A method for producing an olefin-based shrink film, which comprises preheating the sheet at a temperature of 100 to 140°C and stretching it in one direction with a surface temperature difference of 2°C or more between the front and back surfaces of the sheet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24268185A JPS62103128A (en) | 1985-10-31 | 1985-10-31 | Manufacture of olefin series shrink film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24268185A JPS62103128A (en) | 1985-10-31 | 1985-10-31 | Manufacture of olefin series shrink film |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62103128A JPS62103128A (en) | 1987-05-13 |
| JPH0550378B2 true JPH0550378B2 (en) | 1993-07-28 |
Family
ID=17092648
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24268185A Granted JPS62103128A (en) | 1985-10-31 | 1985-10-31 | Manufacture of olefin series shrink film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62103128A (en) |
-
1985
- 1985-10-31 JP JP24268185A patent/JPS62103128A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62103128A (en) | 1987-05-13 |
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