JPH0214935B2 - - Google Patents
Info
- Publication number
- JPH0214935B2 JPH0214935B2 JP57226548A JP22654882A JPH0214935B2 JP H0214935 B2 JPH0214935 B2 JP H0214935B2 JP 57226548 A JP57226548 A JP 57226548A JP 22654882 A JP22654882 A JP 22654882A JP H0214935 B2 JPH0214935 B2 JP H0214935B2
- Authority
- JP
- Japan
- Prior art keywords
- film
- treatment
- resin
- tackifier
- polypropylene resin
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 229920005989 resin Polymers 0.000 claims description 34
- 239000011347 resin Substances 0.000 claims description 34
- -1 polypropylene Polymers 0.000 claims description 25
- 238000000034 method Methods 0.000 claims description 19
- 238000010438 heat treatment Methods 0.000 claims description 17
- 239000004743 Polypropylene Substances 0.000 claims description 13
- 229920001155 polypropylene Polymers 0.000 claims description 13
- 238000010301 surface-oxidation reaction Methods 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 8
- 229920006280 packaging film Polymers 0.000 claims description 8
- 239000012785 packaging film Substances 0.000 claims description 8
- 239000011342 resin composition Substances 0.000 claims description 7
- 230000032683 aging Effects 0.000 claims description 4
- 238000003851 corona treatment Methods 0.000 claims description 4
- 238000002844 melting Methods 0.000 claims description 4
- 230000008018 melting Effects 0.000 claims description 4
- 239000013078 crystal Substances 0.000 claims description 3
- 235000014113 dietary fatty acids Nutrition 0.000 description 9
- 239000000194 fatty acid Substances 0.000 description 9
- 229930195729 fatty acid Natural products 0.000 description 9
- 239000002736 nonionic surfactant Substances 0.000 description 9
- 230000000704 physical effect Effects 0.000 description 5
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 4
- 229920001328 Polyvinylidene chloride Polymers 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 238000011156 evaluation Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 239000005033 polyvinylidene chloride Substances 0.000 description 4
- 238000004804 winding Methods 0.000 description 4
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000005520 cutting process Methods 0.000 description 3
- 150000004665 fatty acids Chemical class 0.000 description 3
- 229920001684 low density polyethylene Polymers 0.000 description 3
- 239000004702 low-density polyethylene Substances 0.000 description 3
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 125000005907 alkyl ester group Chemical group 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 238000010411 cooking Methods 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 235000011187 glycerol Nutrition 0.000 description 2
- DNIAPMSPPWPWGF-UHFFFAOYSA-N monopropylene glycol Natural products CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 2
- 229920000915 polyvinyl chloride Polymers 0.000 description 2
- 239000004800 polyvinyl chloride Substances 0.000 description 2
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 2
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 2
- JNYAEWCLZODPBN-JGWLITMVSA-N (2r,3r,4s)-2-[(1r)-1,2-dihydroxyethyl]oxolane-3,4-diol Chemical compound OC[C@@H](O)[C@H]1OC[C@H](O)[C@H]1O JNYAEWCLZODPBN-JGWLITMVSA-N 0.000 description 1
- ZORQXIQZAOLNGE-UHFFFAOYSA-N 1,1-difluorocyclohexane Chemical compound FC1(F)CCCCC1 ZORQXIQZAOLNGE-UHFFFAOYSA-N 0.000 description 1
- IANQTJSKSUMEQM-UHFFFAOYSA-N 1-benzofuran Chemical compound C1=CC=C2OC=CC2=C1 IANQTJSKSUMEQM-UHFFFAOYSA-N 0.000 description 1
- 239000005995 Aluminium silicate Substances 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 description 1
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical class C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 1
- 239000005909 Kieselgur Substances 0.000 description 1
- 239000004594 Masterbatch (MB) Substances 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 229920002367 Polyisobutene Polymers 0.000 description 1
- 229920001214 Polysorbate 60 Polymers 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000003973 alkyl amines Chemical class 0.000 description 1
- 150000005215 alkyl ethers Chemical class 0.000 description 1
- 125000005037 alkyl phenyl group Chemical group 0.000 description 1
- 235000012211 aluminium silicate Nutrition 0.000 description 1
- AGXUVMPSUKZYDT-UHFFFAOYSA-L barium(2+);octadecanoate Chemical compound [Ba+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O AGXUVMPSUKZYDT-UHFFFAOYSA-L 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- VBICKXHEKHSIBG-UHFFFAOYSA-N beta-monoglyceryl stearate Natural products CCCCCCCCCCCCCCCCCC(=O)OCC(O)CO VBICKXHEKHSIBG-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000740 bleeding effect Effects 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- 239000002981 blocking agent Substances 0.000 description 1
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 1
- 239000008116 calcium stearate Substances 0.000 description 1
- 235000013539 calcium stearate Nutrition 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 1
- HSEMFIZWXHQJAE-UHFFFAOYSA-N hexadecanamide Chemical compound CCCCCCCCCCCCCCCC(N)=O HSEMFIZWXHQJAE-UHFFFAOYSA-N 0.000 description 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- AUHZEENZYGFFBQ-UHFFFAOYSA-N mesitylene Substances CC1=CC(C)=CC(C)=C1 AUHZEENZYGFFBQ-UHFFFAOYSA-N 0.000 description 1
- 125000001827 mesitylenyl group Chemical group [H]C1=C(C(*)=C(C([H])=C1C([H])([H])[H])C([H])([H])[H])C([H])([H])[H] 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- LYRFLYHAGKPMFH-UHFFFAOYSA-N octadecanamide Chemical compound CCCCCCCCCCCCCCCCCC(N)=O LYRFLYHAGKPMFH-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920001083 polybutene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 229920013716 polyethylene resin Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 229920005606 polypropylene copolymer Polymers 0.000 description 1
- 229920001451 polypropylene glycol Polymers 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
- 229920001384 propylene homopolymer Polymers 0.000 description 1
- 229920005604 random copolymer Polymers 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 239000001593 sorbitan monooleate Substances 0.000 description 1
- 235000011069 sorbitan monooleate Nutrition 0.000 description 1
- 229940035049 sorbitan monooleate Drugs 0.000 description 1
- 239000000600 sorbitol Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 150000003505 terpenes Chemical class 0.000 description 1
- 235000007586 terpenes Nutrition 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Landscapes
- Treatments Of Macromolecular Shaped Articles (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
- Wrappers (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
Description
本発明は包装用フイルムの製造方法に関し、詳
しくは自己粘着性(ラツプ性)、耐熱性およびカ
ツト性のいずれにもすぐれた包装用フイルムの製
造方法に関する。
従来、家庭用、業務用に用いられる、いわゆる
ラツプフイルムとしては、ポリ塩化ビニリデン樹
脂や高圧法低密度ポリエチレン樹脂を製膜してな
るフイルムなどが実用化されている。これらラツ
プフイルムとしては、自己粘着性の他に使用時の
カツト性,強度,透明性,耐熱性など種々の性能
が要求されている。
しかしながら、ポリ塩化ビニリデン樹脂やポリ
塩化ビニル樹脂などは塩素を多量に含んでいるた
め、焼却時に塩素ガスを発生したり、多量に含ま
れる可塑剤の有害性などが問題となつている。こ
のため、このような問題点の少ない高圧法低密度
ポリエチレン樹脂も使用されているが、これ自身
自己粘着性が非常に低く、種々の粘着付与剤を添
加しなければならないという欠点があるととも
に、カツト性に劣る欠点がある。
また、ポリ塩化ビニリデン樹脂製ラツプフイル
ムは、二軸延伸されているためカツト時に斜めに
裂けやすく、また電子レンジで加熱した場合など
著しく収縮する。一方、高圧法低密度ポリエチレ
ン樹脂製ラツプフイルムは耐熱性が十分ではな
く、従つて近時めざましく普及している電子レン
ジで調理,加熱する場合に使用すると、フイルム
が溶融して破損したり、あるいはフイルム同士が
融着して破れたり溶融して容器などに付着したり
する欠点があるため、その用途は大幅に制限され
ている。
これらの問題点を解消するものとして、ポリプ
ロピレン系樹脂を用いることも提案されている。
しかしポリプロピレン系樹脂を用いた場合、耐熱
性という点では満足できるものであるが、自己粘
着性やカツト性というラツプフイルムの最も重要
な要求性能を満足することができない。
そこで、自己粘着性を付与するため粘着付与剤
を配合すると自己粘着性は良くなるが、カツト性
が悪く使用に耐えない。また、カツト性の向上を
目的にフイルムを延伸すると粘着付与剤がブリー
ドしなかつたり、あるいはその後配向を緩和させ
てブリードさせても、ブリードした粘着付与剤が
凝集して玉状となりフイルムの透明感や光沢にす
ぐれたフイルムを得ることができず、しかも重ね
合せたフイルムを引きはがした場合界面破壊を生
ずるなどの欠点がある。
したがつて、これまでに自己粘着性とカツト性
のいずれをも満足するポリプロピレン系樹脂から
なるラツプフイルムは得られていない。
本発明はこれら上記の欠点を解消し、ラツプフ
イルムとして好適な包装用フイルムの製造方法を
提供することを目的とするものである。
すなわち本発明は、ポリプロピレン系樹脂に粘
着付与剤を配合した樹脂組成物からなり、かつ少
なくとも横方向に延伸されたフイルムを表面酸化
処理および結晶融点以下であつて、50℃以上の温
度で熱処理した後巻き取り、次いで巻き取られた
フイルムを60〜120℃の温度で30分以上熟成する
ことを特徴とする包装用フイルムの製造方法を提
供するものである。
本発明において用いるポリプロピレン系樹脂の
種類は特に制限はなく、プロピレンホモポリマー
はもちろんエチレン等とプロピレンのコポリマー
であつてもよい。さらにプロピレンとエチレン等
他成分とのコポリマーはランダムコポリマー,ブ
ロツクコポリマーのいずれであつてもよい。な
お、このポリプロピレン系樹脂の物性は各種用
途,条件等に応じて適宜選定すればよいが、通常
はメルトインデツクス(MI)6〜11、密度0.900
〜0.910g/10分のものが好ましい。
次に上記ポリプロピレン系樹脂に配合される粘
着付与剤としては非イオン性界面活性剤あるいは
分子量3000以下の比較的低分子量の樹脂が用いら
れる。
ここで非イオン性界面活性剤としてはアルコー
ルと脂肪酸とのエステルおよびその誘導体を意味
し、ここで用いるアルコールの例としてグリセリ
ン,ポリグリセリン,ソルビタン,ソルビトー
ル,ペンタエリスリトール,ポリエチレングリコ
ール,ポリプロピレングリコールなどがあり、脂
肪酸の例としてアルキル基の炭素数が5〜13個の
直鎖状不飽和脂肪酸,アルキル基の炭素数が17〜
21個の直鎖不飽和脂肪酸などがある。また、該エ
ステルの誘導体としてはエチレンオキシド付加物
などがある。この非イオン性界面活性剤を具体的
に例示すると、ポリオキシエチレンアルキルエー
テル,ポリオキシエチレンアルキルフエニルエー
テル,ポリオキシエチレンアルキルエステル,ポ
リオキシエチレンソルビタンアルキルエステル,
ポリオキシエチレンアルキルアミン,グリセリン
脂肪酸エステル,ソルビタン脂肪酸エステル,ペ
ンタエリスリトール脂肪酸エステル,プロピレン
グリコール脂肪酸エステル,トリメチロールプロ
パン脂肪酸エステル等が挙げられる。
この非イオン性界面活性剤と上記ポリプロピレ
ン系樹脂との配合比は、ポリプロピレン系樹脂
100重量部に対し、非イオン性界面活性剤1〜5
重量部の範囲で用いることが好ましい。非イオン
性界面活性剤の配合量が1重量部未満であると、
十分な自己粘着性が得られず、また5重量部を超
えるとフイルム表面にブリードした非イオン性界
面活性剤が被包装物面に移行するので好ましくな
い。また、非イオン性界面活性剤としては常温に
おいて液状のものが好ましい。
また、分子量3000以下の比較的分子量の樹脂と
しては、例えばテルペン樹脂,クマロン樹脂,ク
マロン―インデン樹脂,キシレン樹脂,メシチレ
ン樹脂,石油樹脂などのほか低重合度ポリオレフ
イン(ポリエチレン,ポリブテン,ポリイソブチ
レンなど)を挙げることができる。この分子量
3000以下の比較的低分子量の樹脂と上記ポリプロ
ピレン系樹脂との配合比は後者100重量部に対し、
前者1〜10重量部の範囲で用いることが好まし
い。
本発明にあつては、まずポリプロピレン系樹脂
に、非イオン性界面活性剤あるいは分子量3000以
下の比較的低分子量の樹脂からなる粘着付与剤を
配合した樹脂組成物をT―ダイ法,インフレーシ
ヨン法などの手段によつて溶融押出製膜して原反
フイルムを製造する。
次いで得られた原反をチユーブラ法,テンター
法などの手段によつて延伸する。本発明において
は原反フイルムを二軸延伸装置などを用いて少な
くとも横方向に延伸しておくことが必要であり、
延伸倍率は横方向に2倍以上、好ましくは3〜6
倍である。このように原反チユーブを少なくとも
横方向に延伸することにより、カツト性や強度が
向上しかも表面状態の良好なフイルムを得ること
ができる。
ここでフイルムの厚みは通常6〜60μ、好まし
くは8〜15μである。
このようにして得られたフイルムはカツト性が
向上したとは言うものの自己粘着性を有せず必ず
しもラツプフイルムとして十分に満足しうるもの
であるとは言えない。
そこで本発明においては、このようにして得ら
れたフイルムをスリツター等で切り開き表面酸化
処理および熱処理した後巻き取り、次いで巻き取
られたフイルムを熟成して包装用フイルムとする
ものである。
本発明においては表面酸化処理と熱処理はいず
れを先に行なつてもよいが、表面酸化処理は巻き
取り前の通常緊張下の状態において行なわれる。
また熱処理は通常弛緩下の状態で行なわれる。
ここで表面酸化処理の方法は特に制限はなく、
コロナ放電処理,火焔処理,オゾン処理,紫外線
処理,酸化性薬液処理等を適用することができ、
とりわけコロナ放電処理が好ましい。表面の酸化
程度は表面酸化処理法などによつて異なり一義的
に決定することは困難である。コロナ放電処理の
場合、表面張力が通常35dyn/cm以上となるよう
に行なうことが好ましい。このような表面酸化処
理により粘着付与剤をフイルム表面に均一にブリ
ードさせることができる。
また、熱処理の方法も特に制限はなく、加熱ロ
ール法,オーブン法等により行なうことができ
る。熱処理条件としては結晶融点以下であつて50
℃以上の温度で行なう。また、熱処理の時間は熱
処理の温度やフイルムの厚み等によつて異なり一
義的に定めることは困難であるが、通常2〜20秒
である。なお、熱処理後は冷却ロール等を用いて
冷却しておくことが好ましい。
このように表面酸化処理および熱処理したフイ
ルムを紙管等に巻き取り、次いで巻き取られたフ
イルムを熟成させる。フイルムの生産性等を考慮
すると60〜120℃の温度で30分以上、好ましくは
90〜110℃で1〜5時間熟成させる。
なお、本発明にあつては前記樹脂組成物中に、
必要により適宜各種の添加剤を加えることもでき
る。添加剤としては滑剤やアンチブロツキング剤
等が挙げられ、具体的にはステアリン酸カルシウ
ム,ステアリン酸バリウムなどの金属石けん、ス
テアリン酸アミド,パルミチン酸アミドなどの脂
肪酸アミド、ステアリン酸モノグリセライドや粉
末シリカ,ケイ藻土,カオリン,タルクなどを例
示することができる。
このような構成からなる本発明の方法によれ
ば、自己粘着性、耐熱性およびカツト性の両特性
を満足するフイルムを得ることができる。
しかも、本発明の方法により得られたフイルム
は延伸配向されているので強度が高く、さらにカ
ツト性にもすぐれており、カツト時に斜めに裂け
ることもない。また、延伸配向によりフイルムの
厚みを薄肉化でき省資源ともなる。
さらに本発明の方法により得られたフイルムは
透明性にすぐれるとともに外観が良好である。し
かも耐熱性にもすぐれており、電子レンジで調
理,加熱する場合に好適に使用することができ、
また焼却廃棄時にポリ塩化ビニリデン樹脂やポリ
塩化ビニル樹脂などのように塩素ガスを発生する
ことがなく、安全性が高いものである。
したがつて、本発明は家庭用ラツプフイルム,
業務用ラツプフイルムなどの包装用フイルムの製
造方法として有用である。
次に、本発明を実施例により説明する。
実施例 1〜4
第1図に示す装置を用いてフイルムを製造し
た。
まず、ポリプロピレン樹脂(密度0.91g/cm3,
MI7g/10分)に第1表に示す粘着付与剤を所定
量配合(マスターバツチ使用)した樹脂組成物を
チユーブ製造押出機1を用いて樹脂温度200℃で
水冷下吹き方法で押出し、径100mm,厚み100μの
原反チユーブ2を得た。得られた原反チユーブを
引き続きチユーブラ法二軸延伸装置3に導入し、
延伸機入口速度2.2m/分,延伸機出口速度8.0
m/分の延伸条件により縦、横それぞれの延伸倍
率が約4倍のフイルム(厚み7μ)を得た。次い
で該フイルムをスリツター4で切り開き、130℃
の加熱ロール5を用いて接触時間4秒の熱処理を
行ない冷却ロールで冷却後、表面張力が38dyn/
cm以上となるようにコロナ放電装置6を用いて表
面酸化処理を行なつた。次いで該フイルムを巻取
装置7を用いて紙管に巻き取り、巻き取られたフ
イルムを熟成装置7(加熱炉)を用いて100℃で
5時間熟成して包装用フイルムを得た。
得られたフイルムの物性,ラツプフイルムとし
ての評価結果を第1表に示す。
比較例 1
ポリプロピレン樹脂(実施例1〜4で用いたと
同じもの)に第1表に示す粘着付与剤を所定量配
合した樹脂組成物を50mmφダイ(リツプ開度0.5
mm)を用いて樹脂温度200℃で水冷下吹き方法で
押出し、径100mm,厚み10μのフイルムを得た。
ムを得た。
得られたフイルムの物性,ラツプフイルムとし
ての評価結果を第1表に示す。
比較例 2〜6
実施例3において、第1表に示す処理工程のみ
行なつたこと以外は実施例3に準じて行ないフイ
ルムを得た。
得られたフイルムの物性,ラツプフイルムとし
ての評価結果を第1表に示す。
比較例 7
高圧法ポリエチレン樹脂(密度0.922g/cm3,
MI5g/10分)にソルビタンモノオレートを1重
量%配合した樹脂組成物をT―ダイ押出機を用い
て温度260℃で成形し、厚み10μのフイルムを得
た。
得られたフイルムの物性,ラツプフイルムとし
ての評価結果を第1表に示す。
The present invention relates to a method for producing a packaging film, and more particularly to a method for producing a packaging film that has excellent self-adhesiveness (wrapping properties), heat resistance, and cutting properties. BACKGROUND ART Conventionally, so-called wrap films used for household and commercial purposes include films made from polyvinylidene chloride resin and high-pressure low-density polyethylene resin. In addition to self-adhesiveness, these wrap films are required to have various properties such as cuttability during use, strength, transparency, and heat resistance. However, since polyvinylidene chloride resins and polyvinyl chloride resins contain large amounts of chlorine, there are problems such as generation of chlorine gas when incinerated and the toxicity of the plasticizers contained in large amounts. For this reason, high-pressure low-density polyethylene resins are also used, which have fewer problems, but they have the disadvantage of having very low self-adhesiveness and the need to add various tackifiers. It has the disadvantage of poor cutability. Furthermore, polyvinylidene chloride resin wrap films are biaxially stretched, so they tend to tear diagonally when cut, and they also shrink significantly when heated in a microwave oven. On the other hand, wrap films made of high-pressure low-density polyethylene resin do not have sufficient heat resistance, so if they are used for cooking or heating in microwave ovens, which are becoming increasingly popular these days, the film may melt and break, or the film may become damaged. Because they have the drawback of being fused together and torn, or melting and adhering to containers, etc., their uses are severely limited. In order to solve these problems, it has also been proposed to use polypropylene resin.
However, when polypropylene resin is used, although it is satisfactory in terms of heat resistance, it cannot satisfy the most important performance requirements of wrap films, such as self-adhesiveness and cutability. Therefore, if a tackifier is added to impart self-adhesive properties, the self-adhesive properties will be improved, but the cutting properties will be poor and the product will not be usable. In addition, when the film is stretched for the purpose of improving cuttability, the tackifier may not bleed, or even if the orientation is relaxed and allowed to bleed, the tackifier that bleeds out aggregates into beads and gives the film a transparent appearance. It is not possible to obtain a film with excellent gloss and gloss, and furthermore, there are drawbacks such as interfacial destruction occurring when the stacked films are peeled off. Therefore, no wrap film made of a polypropylene resin that satisfies both self-adhesiveness and cuttability has so far been obtained. The object of the present invention is to eliminate these above-mentioned drawbacks and provide a method for producing a packaging film suitable as a wrap film. That is, the present invention consists of a resin composition in which a tackifier is blended with a polypropylene resin, and a film stretched at least in the transverse direction is subjected to surface oxidation treatment and heat treatment at a temperature below the crystal melting point and above 50°C. The present invention provides a method for producing a packaging film, which comprises post-winding and then aging the wound film at a temperature of 60 to 120°C for 30 minutes or more. The type of polypropylene resin used in the present invention is not particularly limited, and may be a propylene homopolymer or a copolymer of ethylene or the like and propylene. Further, the copolymer of propylene and other components such as ethylene may be either a random copolymer or a block copolymer. Note that the physical properties of this polypropylene resin may be selected appropriately depending on various uses and conditions, but usually it has a melt index (MI) of 6 to 11 and a density of 0.900.
~0.910g/10 minutes is preferred. Next, as the tackifier added to the polypropylene resin, a nonionic surfactant or a relatively low molecular weight resin of 3000 or less is used. Here, nonionic surfactants refer to esters of alcohol and fatty acids and their derivatives, and examples of alcohols used here include glycerin, polyglycerin, sorbitan, sorbitol, pentaerythritol, polyethylene glycol, and polypropylene glycol. Examples of fatty acids include linear unsaturated fatty acids with an alkyl group of 5 to 13 carbon atoms, and alkyl groups with 17 to 13 carbon atoms.
There are 21 straight chain unsaturated fatty acids. Furthermore, derivatives of the esters include ethylene oxide adducts and the like. Specific examples of this nonionic surfactant include polyoxyethylene alkyl ether, polyoxyethylene alkyl phenyl ether, polyoxyethylene alkyl ester, polyoxyethylene sorbitan alkyl ester,
Examples include polyoxyethylene alkylamine, glycerin fatty acid ester, sorbitan fatty acid ester, pentaerythritol fatty acid ester, propylene glycol fatty acid ester, trimethylolpropane fatty acid ester, and the like. The blending ratio of this nonionic surfactant and the above polypropylene resin is
1 to 5 parts of nonionic surfactant per 100 parts by weight
It is preferable to use within the range of parts by weight. When the amount of nonionic surfactant is less than 1 part by weight,
Sufficient self-adhesiveness cannot be obtained, and if the amount exceeds 5 parts by weight, the nonionic surfactant that bleeds onto the surface of the film will transfer to the surface of the packaged object, which is not preferable. Moreover, as the nonionic surfactant, one that is liquid at room temperature is preferable. In addition, examples of resins with a relatively molecular weight of 3000 or less include terpene resins, coumaron resins, coumaron-indene resins, xylene resins, mesitylene resins, petroleum resins, and low polymerization degree polyolefins (polyethylene, polybutene, polyisobutylene, etc.). can be mentioned. This molecular weight
The blending ratio of relatively low molecular weight resin of 3000 or less and the above polypropylene resin is 100 parts by weight of the latter,
The former is preferably used in a range of 1 to 10 parts by weight. In the present invention, first, a resin composition in which a tackifier consisting of a nonionic surfactant or a relatively low molecular weight resin with a molecular weight of 3,000 or less is blended with a polypropylene resin is prepared by a T-die method or an inflation process. A raw film is produced by melt extrusion film formation by a method such as a method. Next, the obtained original fabric is stretched by a tubular method, a tenter method, or the like. In the present invention, it is necessary to stretch the original film at least in the transverse direction using a biaxial stretching device or the like.
The stretching ratio is 2 times or more in the transverse direction, preferably 3 to 6
It's double. By stretching the raw tube at least in the transverse direction in this way, it is possible to obtain a film with improved cuttability and strength and a good surface condition. The thickness of the film is usually 6 to 60 microns, preferably 8 to 15 microns. Although the film thus obtained has improved cutting properties, it does not have self-adhesion and cannot necessarily be said to be fully satisfactory as a wrap film. Therefore, in the present invention, the film thus obtained is cut open with a slitter or the like, subjected to surface oxidation treatment and heat treatment, and then wound up, and then the wound up film is aged to produce a packaging film. In the present invention, either the surface oxidation treatment or the heat treatment may be performed first, but the surface oxidation treatment is usually performed under tension before winding.
Further, heat treatment is usually carried out in a relaxed state. There is no particular restriction on the method of surface oxidation treatment;
Corona discharge treatment, flame treatment, ozone treatment, ultraviolet treatment, oxidizing chemical treatment, etc. can be applied.
Particularly preferred is corona discharge treatment. The degree of oxidation on the surface varies depending on the surface oxidation treatment method, etc., and is difficult to determine unambiguously. In the case of corona discharge treatment, it is preferable to carry out the treatment so that the surface tension is usually 35 dyn/cm or more. Such surface oxidation treatment allows the tackifier to bleed uniformly onto the film surface. Further, the method of heat treatment is not particularly limited, and may be carried out by a heated roll method, an oven method, or the like. The heat treatment conditions are below the crystal melting point and 50
Perform at a temperature of ℃ or above. Further, the heat treatment time varies depending on the heat treatment temperature, the thickness of the film, etc., and is difficult to determine unambiguously, but is usually 2 to 20 seconds. Note that after the heat treatment, it is preferable to cool the film using a cooling roll or the like. The film subjected to the surface oxidation treatment and heat treatment is wound up into a paper tube or the like, and then the wound film is aged. Considering film productivity, etc., at a temperature of 60 to 120°C for 30 minutes or more, preferably
Maturing at 90-110℃ for 1-5 hours. In addition, in the present invention, in the resin composition,
Various additives can also be added as appropriate. Examples of additives include lubricants and anti-blocking agents, including metal soaps such as calcium stearate and barium stearate, fatty acid amides such as stearic acid amide and palmitic acid amide, stearic acid monoglyceride, powdered silica, Examples include diatomaceous earth, kaolin, and talc. According to the method of the present invention having such a configuration, it is possible to obtain a film that satisfies both properties of self-adhesiveness, heat resistance, and cuttability. Moreover, since the film obtained by the method of the present invention is stretched and oriented, it has high strength and also has excellent cuttability, and does not tear diagonally when cut. Furthermore, the thickness of the film can be reduced by stretching and orientation, resulting in resource savings. Furthermore, the film obtained by the method of the present invention has excellent transparency and good appearance. Moreover, it has excellent heat resistance, making it suitable for use when cooking and heating in a microwave oven.
Furthermore, when disposed of by incineration, it does not generate chlorine gas unlike polyvinylidene chloride resin or polyvinyl chloride resin, making it highly safe. Therefore, the present invention provides household wrapping film,
This method is useful as a method for producing packaging films such as wrap films for commercial use. Next, the present invention will be explained by examples. Examples 1 to 4 Films were manufactured using the apparatus shown in FIG. First, polypropylene resin (density 0.91g/cm 3 ,
A resin composition prepared by blending a predetermined amount (using a master batch) of the tackifier shown in Table 1 with MI7g/10 minutes) was extruded using a tube manufacturing extruder 1 at a resin temperature of 200°C using a water-cooled downward blowing method, and the diameter was 100mm. A raw tube 2 having a thickness of 100 μm was obtained. The obtained original fabric tube was then introduced into the tubular method biaxial stretching device 3,
Stretching machine entrance speed 2.2m/min, stretching machine exit speed 8.0
A film (thickness: 7 μm) with a stretching ratio of about 4 times in both the longitudinal and transverse directions was obtained under the stretching conditions of m/min. Next, the film was cut open with a slitter 4 and heated to 130°C.
Heat treatment was performed using a heating roll 5 for a contact time of 4 seconds, and after cooling with a cooling roll, the surface tension became 38 dyn/
A surface oxidation treatment was performed using a corona discharge device 6 so that the thickness was at least cm. Next, the film was wound up into a paper tube using the winding device 7, and the wound film was aged at 100° C. for 5 hours using the aging device 7 (heating furnace) to obtain a packaging film. Table 1 shows the physical properties of the obtained film and the evaluation results as a wrapped film. Comparative Example 1 A resin composition prepared by blending a predetermined amount of the tackifier shown in Table 1 with polypropylene resin (the same as used in Examples 1 to 4) was heated in a 50 mmφ die (rip opening degree 0.5).
A film with a diameter of 100 mm and a thickness of 10 μm was obtained by extrusion using a water-cooled downward blowing method at a resin temperature of 200°C. I got it. Table 1 shows the physical properties of the obtained film and the evaluation results as a wrapped film. Comparative Examples 2 to 6 Films were obtained in the same manner as in Example 3, except that only the treatment steps shown in Table 1 were carried out. Table 1 shows the physical properties of the obtained film and the evaluation results as a wrapped film. Comparative Example 7 High-pressure polyethylene resin (density 0.922 g/cm 3 ,
A resin composition containing 1% by weight of sorbitan monooleate (MI5g/10min) was molded using a T-die extruder at a temperature of 260°C to obtain a film with a thickness of 10μ. Table 1 shows the physical properties of the obtained film and the evaluation results as a wrapped film.
【表】【table】
【表】
*4 ポリグリセリン脂肪酸エステル〓
〓B:HLB6.2
なお、上記比較例6においては、ブリードした
粘着付与剤が凝集してフイルム表面にまだら模様
が発生した。[Table] *4 Polyglycerin fatty acid ester
〓B:HLB6.2
In Comparative Example 6, the bleeding tackifier aggregated and a mottled pattern appeared on the film surface.
第1図は本発明の方法に用いる装置の概略図で
ある。
1……チユーブ製造押出機、2……原反チユー
ブ、3……二軸延伸装置、4……スリツター、5
……加熱ロール、6……コロナ放電装置、7……
巻取装置、8……熟成装置。
FIG. 1 is a schematic diagram of the apparatus used in the method of the invention. DESCRIPTION OF SYMBOLS 1...Tube manufacturing extruder, 2... Raw tube, 3... Biaxial stretching device, 4... Slitter, 5
... Heating roll, 6 ... Corona discharge device, 7 ...
Winding device, 8... aging device.
Claims (1)
た樹脂組成物からなり、かつ少なくとも横方向に
延伸されたフイルムを表面酸化処理および結晶融
点以下であつて、50℃以上の温度で熱処理した後
巻き取り、次いで巻き取られたフイルムを60〜
120℃の温度で30分以上熟成することを特徴とす
る包装用フイルムの製造方法。 2 表面酸化処理がコロナ放電処理である特許請
求の範囲第1項記載の方法。[Claims] 1. A film made of a resin composition containing a tackifier blended with a polypropylene resin and stretched at least in the transverse direction is surface oxidized and heated at a temperature below the crystal melting point and above 50°C. After heat treatment, the film is rolled up, and then the rolled film is heated for 60~
A method for producing a packaging film characterized by aging at a temperature of 120°C for 30 minutes or more. 2. The method according to claim 1, wherein the surface oxidation treatment is a corona discharge treatment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22654882A JPS59120635A (en) | 1982-12-27 | 1982-12-27 | Production of packaging film |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22654882A JPS59120635A (en) | 1982-12-27 | 1982-12-27 | Production of packaging film |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59120635A JPS59120635A (en) | 1984-07-12 |
JPH0214935B2 true JPH0214935B2 (en) | 1990-04-10 |
Family
ID=16846874
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22654882A Granted JPS59120635A (en) | 1982-12-27 | 1982-12-27 | Production of packaging film |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59120635A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0698486A1 (en) | 1994-07-13 | 1996-02-28 | Sumitomo Chemical Company, Limited | Self-tacky packaging film |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6858288B2 (en) | 2000-05-23 | 2005-02-22 | Oji Paper Co., Ltd. | Wrap film |
WO2006019544A1 (en) * | 2004-07-13 | 2006-02-23 | Exxonmobil Chemical Patents Inc. | Improved surface treatment of polymeric articles |
JP2009096499A (en) * | 2007-10-16 | 2009-05-07 | Okamoto Ind Inc | Household wrapping film |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5125547A (en) * | 1974-08-28 | 1976-03-02 | Mitsubishi Chem Ind | |
JPS52152468A (en) * | 1976-06-15 | 1977-12-17 | Mitsubishi Chem Ind | Method of manufacture of polyolefine film |
-
1982
- 1982-12-27 JP JP22654882A patent/JPS59120635A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5125547A (en) * | 1974-08-28 | 1976-03-02 | Mitsubishi Chem Ind | |
JPS52152468A (en) * | 1976-06-15 | 1977-12-17 | Mitsubishi Chem Ind | Method of manufacture of polyolefine film |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0698486A1 (en) | 1994-07-13 | 1996-02-28 | Sumitomo Chemical Company, Limited | Self-tacky packaging film |
Also Published As
Publication number | Publication date |
---|---|
JPS59120635A (en) | 1984-07-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0450088B1 (en) | Biaxially oriented polyethylene film | |
EP0045580A1 (en) | Heat-sealable polypropylene blends and methods for their preparation | |
US3194863A (en) | Compression rolling of multiple strips of organic polymers | |
TW584592B (en) | A method for producing biaxially stretched film made of ethylene-vinyl alcohol copolymer | |
JPS6147234A (en) | Manufacturing method of heat shrinkable polypropylene film | |
JPH01120339A (en) | Heat shrinkable film for packing and preparation thereof | |
JP2000026623A5 (en) | ||
JP2000026623A (en) | Adhering heat-resistant wrapping film | |
JPH0214935B2 (en) | ||
JPH0899393A (en) | Polyolefinic heat-shrinkable laminated film | |
JPH11348205A (en) | Multi-layered shrink film | |
JP2000026624A (en) | Adhering heat-resistant wrapping film | |
JP2535061B2 (en) | Film production method | |
JP4338715B2 (en) | Adhesive heat-resistant wrap film | |
JP2002348445A (en) | Biodegradable plastic packaging band and method for producing the same | |
JPH1199600A (en) | Polyolefinic laminated stretch shrink film | |
JPH05177784A (en) | Heat-shrinkable multilayered film | |
CA2032272C (en) | Improved heat shrinkable polyolefin film | |
JPH02127022A (en) | Film for twist wrapping | |
JP2000026625A (en) | Adhering heat-resistant wrapping film | |
JP4731407B2 (en) | Biodegradable heat shrinkable laminated film | |
JP2798236B2 (en) | Multi-layer shrink film and manufacturing method thereof | |
JPH0441902B2 (en) | ||
JP3789652B2 (en) | Heat resistant adhesive wrap film | |
JPH11116787A (en) | Wrap film |