JPH02139220A - White polyolefin film and manufacture thereof - Google Patents
White polyolefin film and manufacture thereofInfo
- Publication number
- JPH02139220A JPH02139220A JP29429988A JP29429988A JPH02139220A JP H02139220 A JPH02139220 A JP H02139220A JP 29429988 A JP29429988 A JP 29429988A JP 29429988 A JP29429988 A JP 29429988A JP H02139220 A JPH02139220 A JP H02139220A
- Authority
- JP
- Japan
- Prior art keywords
- film
- stretching
- temperature
- polyolefin film
- stretched
- 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
- 229920000098 polyolefin Polymers 0.000 title claims abstract description 19
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 claims abstract description 23
- -1 polypropylene Polymers 0.000 claims abstract description 18
- 230000003287 optical effect Effects 0.000 claims abstract description 17
- 229920000642 polymer Polymers 0.000 claims abstract description 12
- 239000004743 Polypropylene Substances 0.000 claims abstract description 11
- 229920001155 polypropylene Polymers 0.000 claims abstract description 11
- 229920005989 resin Polymers 0.000 claims abstract description 10
- 239000011347 resin Substances 0.000 claims abstract description 10
- 238000000605 extraction Methods 0.000 claims abstract description 8
- 238000000034 method Methods 0.000 abstract description 12
- JMMZCWZIJXAGKW-UHFFFAOYSA-N 2-methylpent-2-ene Chemical compound CCC=C(C)C JMMZCWZIJXAGKW-UHFFFAOYSA-N 0.000 abstract description 5
- 229920001577 copolymer Polymers 0.000 description 11
- 238000012545 processing Methods 0.000 description 8
- 239000000203 mixture Substances 0.000 description 6
- 238000004806 packaging method and process Methods 0.000 description 6
- 239000002932 luster Substances 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- 229920005629 polypropylene homopolymer Polymers 0.000 description 5
- WSSSPWUEQFSQQG-UHFFFAOYSA-N 4-methyl-1-pentene Chemical compound CC(C)CC=C WSSSPWUEQFSQQG-UHFFFAOYSA-N 0.000 description 4
- 235000009508 confectionery Nutrition 0.000 description 4
- 229920001519 homopolymer Polymers 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 238000004080 punching Methods 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 3
- 238000005034 decoration Methods 0.000 description 3
- 235000011888 snacks Nutrition 0.000 description 3
- CXWXQJXEFPUFDZ-UHFFFAOYSA-N tetralin Chemical compound C1=CC=C2CCCCC2=C1 CXWXQJXEFPUFDZ-UHFFFAOYSA-N 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000003851 corona treatment Methods 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000010954 inorganic particle Substances 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 238000000691 measurement method Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- 229920005604 random copolymer Polymers 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000037303 wrinkles Effects 0.000 description 2
- 239000004711 α-olefin Substances 0.000 description 2
- 101100402795 Caenorhabditis elegans mtl-1 gene Proteins 0.000 description 1
- 229920000298 Cellophane Polymers 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000002390 adhesive tape Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000002216 antistatic agent Substances 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
- 238000009835 boiling Methods 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000003484 crystal nucleating agent Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229920005674 ethylene-propylene random copolymer Polymers 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003475 inorganic filler Inorganic materials 0.000 description 1
- 229920000554 ionomer Polymers 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000003348 petrochemical agent Substances 0.000 description 1
- 238000009832 plasma treatment Methods 0.000 description 1
- 229920005606 polypropylene copolymer Polymers 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、白色不透明で、擬紙状光、沢、パール調光沢
をもつポリオレフィンフィルムで、各種印刷性、寸法安
定性、耐水性(湿気)、耐薬品性の要求される印刷用紙
、各種ラベル、菓子、スナック等の包装および装飾用と
して好適な白色ポリオレフィンフィルムおよびその製造
方法に関する。Detailed Description of the Invention [Industrial Field of Application] The present invention is a polyolefin film that is white and opaque, has a paper-like luster, luster, and pearlescent luster, and has various printability, dimensional stability, and water resistance (moisture resistance). ), relates to a white polyolefin film suitable for packaging and decoration of printing paper, various labels, confectionery, snacks, etc. that requires chemical resistance, and a method for producing the same.
[従来の技術]
従来、白色フィルムを1qるために白色の無機粒子を熱
可塑性樹脂に多量に添加し、−軸又は二軸に延伸するこ
とはよく知られている(特公昭46−40794号公報
、特開昭50−90644等)。このフィルムが白色、
不透明になるのは、フィルム延伸時に樹脂と無機粒子の
界面に剥離がおこり、微細なボイドがフィルム内部に生
成されることおよび表面では微少な亀裂が生成されるこ
とによって光がフィルム表面及び内部で散乱されるため
である。[Prior Art] It is well known that in order to obtain 1 q of white film, a large amount of white inorganic particles are added to a thermoplastic resin and then stretched in the -axis or biaxial direction (Japanese Patent Publication No. 46-40794). Publication, JP-A-50-90644, etc.). This film is white,
The reason why the film becomes opaque is that peeling occurs at the interface between the resin and inorganic particles during film stretching, creating minute voids inside the film and minute cracks on the surface, which prevents light from passing through the film surface and inside. This is because they are scattered.
また、ポリプロピレンあるいはプロピレンコポリマーに
メチルペンチッポリマーをブレンドし、二軸延伸する技
術が知られている(特開昭52−58773.52−5
8774等)。In addition, a technique is known in which polypropylene or propylene copolymer is blended with methyl pentyl polymer and biaxially stretched (Japanese Patent Laid-Open No. 52-58773.52-5
8774 etc.).
(発明が解決しようとする課題]
白色フィルムを得るために、無懇粒子を多聞に添加した
フィルムは、印刷、打法き、自動包装等の二次加工を行
なう場合、表面亀裂によって生じた表面遊離粒子が印刷
の仕上りを著しく低下させ、また内部ボイドが多く生成
させるため機械強度が劣り、二次加工の能率を著しく低
下させるという欠点がある。(Problems to be Solved by the Invention) In order to obtain a white film, a film to which a large amount of non-containing particles have been added may suffer from surface cracks caused by surface cracks when undergoing secondary processing such as printing, punching, automatic packaging, etc. There are disadvantages in that the loose particles significantly deteriorate the printing finish, and since many internal voids are generated, the mechanical strength is poor and the efficiency of secondary processing is significantly reduced.
また、ポリプロピレンにメチルペンチッポリマーをブレ
ンドして、従来の一軸および二軸延伸法にて延伸したフ
ィルムは、粗面化および引裂性は得られるが、成紙状で
、白く、隠蔽性が高く2機械強度の高いフィルムは得ら
れない。In addition, films made by blending polypropylene with methyl pentyl polymer and stretching using conventional uniaxial and biaxial stretching methods have a rough surface and tearability, but are paper-like, white, and have high hiding properties. 2. A film with high mechanical strength cannot be obtained.
本発明は、白色ポリオレフィンフィルムに関し鋭意検討
の結果、白くて隠蔽性に優れ、パール調の光沢を持ち、
機械強度が高く、各種印刷用紙。As a result of extensive research into white polyolefin films, the present invention has revealed that they are white, have excellent hiding properties, have a pearl-like luster,
Various printing papers with high mechanical strength.
各種ラベル、菓子やスナック等の包装および装飾用とし
て好適な白色ポリオレフィンフィルムおよびその製造方
法を提供せんとするものである。It is an object of the present invention to provide a white polyolefin film suitable for various labels, packaging and decoration of confectionery and snacks, and a method for producing the same.
[課題を解決するための手段]
本発明は、光学濃度(OD>が0.1以上、光沢度が4
0%以上のポリオレフィンフィルムであって、該フィル
ムの長手方向の強度が8Krj/mTl1以上で、長手
方向と幅方向のヤング率の和が250Kfl/mTd以
上であることを特徴とする白色ポリオレフィンフィルム
に関するもので、さらに該白色ポリオレフィンフィルム
を得るために、アイソタクチックインデックス(I I
>が80%以上、極限粘度が1.2〜3.5dl/aの
ポリプロピレン100重量部に、n−ヘプタン抽出残分
が40%以上であるメチルペンチッポリマーを5〜50
ffi間部添加してなる樹脂をシート状またはチューブ
状に溶融成形1炎、120℃以下の温度で、弾性限度内
での微延伸をした後、さらに120℃〜170′Cの温
度ですくなくとも一軸に延伸することを特徴とする白色
ポリオレフィンフィルムの製造方法に関するもので必る
。[Means for Solving the Problems] The present invention provides an optical density (OD> of 0.1 or more and a gloss level of 4).
0% or more, the film has a strength in the longitudinal direction of 8 Krj/mTl or more, and a sum of Young's moduli in the longitudinal direction and the width direction of 250 Kfl/mTd or more. Furthermore, in order to obtain the white polyolefin film, the isotactic index (II
>80% or more and an intrinsic viscosity of 1.2 to 3.5 dl/a, to 100 parts by weight of polypropylene with an n-heptane extraction residue of 40% or more, 5 to 50
After melt-molding the resin containing ffi into a sheet or tube at a temperature of 120°C or less within the elastic limit, it is further stretched at least uniaxially at a temperature of 120°C to 170'C. It relates to a method for producing a white polyolefin film, which is characterized by stretching the film.
本発明において、フィルムの光学濃度(OD〉は0.1
以上、好ましくは0.3以上である。光学濃度(OD>
が0.1以下では白さと隠蔽性に劣り、印刷文字や絵が
裏面から見えたりして実用性に劣る。In the present invention, the optical density (OD) of the film is 0.1
It is preferably 0.3 or more. Optical density (OD>
If it is less than 0.1, the whiteness and concealment properties will be poor, and the printed characters and pictures will be visible from the back side, resulting in poor practicality.
また光沢度は40%以上、好ましくは50%以上である
。光沢度が40%以下では、フィルム表面の粗さが大き
く、印刷した際にインキのにじみがおこり鮮明な文字や
絵が得られず、また該フィルムの特徴の一つでおる真珠
様の優雅で高貴な光沢観を損ねてしまう。Moreover, the glossiness is 40% or more, preferably 50% or more. If the gloss level is less than 40%, the surface of the film will be very rough and the ink will bleed when printed, making it difficult to obtain clear letters and pictures. It spoils the noble luster.
さらに本発明フィルムの長手方向の強度は8Kg/mT
d以上、好ましくは10Kg/rrlyy1以上である
。Furthermore, the strength of the film of the present invention in the longitudinal direction is 8Kg/mT.
d or more, preferably 10 Kg/rrlyy1 or more.
長手方向の強度が8Ky/mrd以下では、印刷加工時
にフィルムが寸法変形したり、破れたりして二次加工の
能率が著しく低下してしまう。If the strength in the longitudinal direction is less than 8 Ky/mrd, the film may undergo dimensional deformation or tear during printing, resulting in a significant decrease in the efficiency of secondary processing.
また、フィルムの長手方向と幅方向のヤング率の和は2
50に!J/mTl1以上、好ましくは300 Kg/
mm以上である。ヤング率が250にび7mTl1以下
では印刷加工時にフィルム端部がたるみ、中央部と端部
で印字のずれが起こったり、ラベル用途においては打扱
き加工性やハンドリング性に劣り、さらに包装用として
用いた場合には形態保持性が悪く、内容物保護性に劣る
。Also, the sum of Young's modulus in the longitudinal direction and width direction of the film is 2
To 50! J/mTl1 or more, preferably 300 Kg/
mm or more. If the Young's modulus is less than 250 and 7mTl1, the edges of the film will sag during printing, misalignment of print will occur between the center and the edges, and the processing and handling properties will be poor in label applications, and the film will not be used for packaging. If it is, the shape retention property is poor and the content protection property is poor.
なお、本発明フィルムの密度は0.7g/ff1以上、
好ましくは0.8g/a+f以上のものが良い。Note that the density of the film of the present invention is 0.7 g/ff1 or more,
Preferably, it is 0.8 g/a+f or more.
密度が0.7g/crjより小さいと、フィルム中のボ
イド容積が多く、生産性や機械強度などが劣ることが多
いためである。This is because if the density is less than 0.7 g/crj, the volume of voids in the film is large, and productivity, mechanical strength, etc. are often poor.
また、印刷適性、ラベルなどの打扱き加工、自動包装な
どの二次加工性において本発明のフィルムの厚さは、5
〜100μm1好ましくは10〜60μmである。上記
範囲よりも薄いと隠蔽性や強度および形態保持性などが
不足し、厚いと加工性、ハンドリング性などから好まし
くない。In addition, the thickness of the film of the present invention is 5% in terms of printing suitability, handling processing such as labels, and secondary processing properties such as automatic packaging.
~100 μm, preferably 10 to 60 μm. If it is thinner than the above range, it will lack hiding power, strength, shape retention, etc., and if it is thicker, it will be unfavorable in terms of processability, handling, etc.
本発明でいうポリオレフィンとは、ポリプロピレンホモ
ポリマーまたはコポリマーとメチルペンチッポリマーま
たはコポリマーとの混合物である。The polyolefin as used in the present invention is a mixture of a polypropylene homopolymer or copolymer and a methyl pentyl polymer or copolymer.
ポリプロピレンおよびメチルペンテンは用途によっで使
い分けることが出来、耐熱性、薇械的性質が重視される
場合はホモポリマーで、逆にソフト性、柔軟性を重視す
る場合はコポリマーがよい。Polypropylene and methylpentene can be used depending on the purpose. Homopolymers are preferable when heat resistance and mechanical properties are important, while copolymers are preferable when softness and flexibility are important.
またコポリマーである場合には、他のα−オレフ゛イン
とのランダムまたはブロック共重合体であり、共重合型
としては10モル%以下としておくことが好ましい。さ
らに他の樹脂をブレンドする場合には、ブレンド率は1
Qwt%以下であることが好ましい。If it is a copolymer, it is a random or block copolymer with other α-olefins, and as a copolymer, it is preferably 10 mol% or less. When further blending other resins, the blending ratio is 1
It is preferable that it is Qwt% or less.
次に本発明フィルムの製造方法について述べる。Next, a method for producing the film of the present invention will be described.
該ポリプロピレンまたはコポリマーのアイソタクチック
インデックス(以下IIと略す)は80%以上であるこ
とが必要であり、耐熱性、耐溶剤性が必要である場合に
は、IIが90%以上であると好ましい。The isotactic index (hereinafter abbreviated as II) of the polypropylene or copolymer must be 80% or more, and if heat resistance and solvent resistance are required, II is preferably 90% or more. .
また該ポリプロピレンの極限粘度[ηコは1゜2dl/
g〜3.5dl/aであることが必要であり、好ましく
は1.5dl/a〜2.2d110である。[η]が上
記範囲より小さいと、特にキャスト性、延伸性が悪化し
、大きいと溶融押出し性が悪化するばかりか、製膜も難
しくなる。In addition, the intrinsic viscosity of the polypropylene [η is 1°2 dl/
g to 3.5 dl/a, preferably 1.5 dl/a to 2.2 dl/a. When [η] is smaller than the above range, castability and stretchability are particularly deteriorated, and when it is larger, not only melt extrudability is deteriorated, but also film formation becomes difficult.
次に、該ポリプロピレンまたはコポリマーにブレンドさ
れるメチルペンチッポリマーとは、メチルペンテンホモ
ポリマーまたはコポリマーであって、4メチル1ペンテ
ン単独の重合体または、他のα−オレフィンとのランダ
ム共重合体でおり、4メチル1ペンテンモノマーユニツ
トが80モル%以上のものである。該ポリマーのn−ヘ
プタン抽出残分は40%以上であることが必要であり、
好ましくは50%以上である。n−ヘプタン抽出残分が
40%に満たない場合、光学濃度(OD)が0.1以下
となって、白さおよび隠蔽性が発現しない。また、該ポ
リマーの融点(Tm)は2゜0〜240℃、結晶化温度
(TmC)は180〜220℃であると光学濃度(OD
)が0.1以上となって、白さおよび隠蔽性は良好とな
る。また、分散性の点で、該ポリマーのMlは、2〜2
00g/10分、好ましくは10〜100g/lo分で
あると、光沢度が高くなって好ましい。 該メチルペン
チッポリマーの添加量は、該ポリプロピレン100重量
部に対して、5〜50重量部、好ましくは10〜40重
量部の範囲が良い。5重量部以下では光学濃度(OD)
が小さくなって、白さと隠蔽性に劣り、50重量部以上
では分散性が悪くなって延伸が不安定になり、フィルム
内部に過ボイドができて■械的性賀に劣ったものとなる
。Next, the methyl pentyl polymer blended into the polypropylene or copolymer is a methyl pentene homopolymer or copolymer, and is a polymer of 4 methyl 1 pentene alone or a random copolymer with other α-olefins. The content of 4-methyl-1-pentene monomer units is 80 mol% or more. It is necessary that the n-heptane extraction residue of the polymer is 40% or more,
Preferably it is 50% or more. If the n-heptane extraction residue is less than 40%, the optical density (OD) will be 0.1 or less, and whiteness and hiding properties will not be achieved. Furthermore, when the melting point (Tm) of the polymer is 2°0 to 240°C and the crystallization temperature (TmC) is 180 to 220°C, the optical density (OD
) is 0.1 or more, and the whiteness and hiding properties are good. In addition, in terms of dispersibility, the Ml of the polymer is 2 to 2.
00 g/10 minutes, preferably 10 to 100 g/1 minute, is preferable because the gloss becomes high. The amount of the methyl pentyl polymer added is preferably in the range of 5 to 50 parts by weight, preferably 10 to 40 parts by weight, based on 100 parts by weight of the polypropylene. Optical density (OD) below 5 parts by weight
If the amount exceeds 50 parts by weight, dispersibility becomes poor and stretching becomes unstable, excessive voids are formed inside the film, resulting in poor mechanical properties.
また、本発明フィルムには本目的を損ねない範囲で、結
晶核剤、酸化防止剤、熱安定剤、滑剤、帯電防止剤等を
添加しても良い。Further, crystal nucleating agents, antioxidants, heat stabilizers, lubricants, antistatic agents, etc. may be added to the film of the present invention within a range that does not impair the purpose.
次に、上記混合樹脂を260℃〜310℃に加熱された
押出機に供給し、シート状またはチューブ状に溶融成形
した後、該シートまたはチューブを120℃以下の温度
で弾性限界内の微延伸をした後、さらに120℃〜17
0℃の温度ですくなくとも一軸に延伸することが必要で
ある。公知のステンター式逐次あるいは同時二輪延伸法
あるいは、チューブ式同時二輪延伸法のみによる延伸で
は、本発明の目的である光学濃度(OD)が0゜1以上
の白くて隠蔽性の高いフィルムが得られないためである
。Next, the mixed resin is supplied to an extruder heated to 260°C to 310°C, melt-molded into a sheet or tube, and then slightly stretched within the elastic limit at a temperature of 120°C or lower. After that, further heat to 120℃~17
It is necessary to stretch at least uniaxially at a temperature of 0°C. By stretching only by the known stenter-type sequential or simultaneous two-wheel stretching method or tube-type simultaneous two-wheel stretching method, a white, highly opaque film with an optical density (OD) of 0°1 or more, which is the object of the present invention, cannot be obtained. This is because there is no
弾性限界内での微延伸とは、延伸温度における3t r
ess−stra inカーブの降伏点応力までの延伸
をいう。Slight stretching within the elastic limit means 3t r at the stretching temperature.
Ess-strain refers to the stretching of an in-curve to the yield point stress.
弾性限界内での微延伸の有効な理由は、基本的に非相溶
な樹脂であるポリプロピレンとメチルペンチッポリマー
の混合シート中の海鳥構造を大きくし、両者の界面に微
小ボイドを生成させ、両者の屈折率差による界面乱反射
を大きくして、白さと隠蔽性を発現させるのである。The effective reason for slight stretching within the elastic limit is to increase the size of the seabird structure in the mixed sheet of polypropylene and methyl pentyl polymer, which are basically incompatible resins, and to generate microvoids at the interface between the two. By increasing the diffused reflection at the interface due to the difference in refractive index between the two, whiteness and concealment properties are achieved.
弾性限界内の微延伸後の延伸においては、−軸延伸の場
合、ロール間の周速差による延伸法またはステンター式
延伸法により、延伸温度が120℃〜170℃で、延伸
倍率は面倍率で3〜10倍、好ましくは4〜8倍である
と製膜性が良好となる。In the stretching after slight stretching within the elastic limit, in the case of -axial stretching, the stretching temperature is 120°C to 170°C, and the stretching ratio is the areal ratio by a stretching method using a peripheral speed difference between rolls or a stenter type stretching method. Film formability becomes good in it being 3 to 10 times, preferably 4 to 8 times.
また二輪延伸の場合は、ステンター式逐次あるいは同時
二輪延伸法、またはチューブ式同時二軸延伸法により二
輪延伸される。同時二軸延伸の場合、延伸温度は145
〜165℃の範囲が製膜性が良好となるので好ましく、
延伸倍率は面倍率で10〜50倍、好ましくは20〜4
0倍であると製膜安定性が良好となり、光沢度も高くな
る。In the case of two-wheel stretching, two-wheel stretching is carried out by a stenter type sequential or simultaneous two-wheel stretching method, or a tube type simultaneous biaxial stretching method. In the case of simultaneous biaxial stretching, the stretching temperature is 145
It is preferable that the temperature range is from 165° C. to 165° C. because the film forming property is good.
The stretching ratio is 10 to 50 times, preferably 20 to 4
If it is 0 times, the film forming stability will be good and the gloss will be high.
また逐次二輪延伸の場合、120〜150℃の延伸温度
にて3〜7倍長手方向に延伸し引続きステンターにて1
50〜170℃の延伸温度で幅方向に5〜15倍延伸す
る。In the case of sequential two-wheel stretching, it is stretched 3 to 7 times in the longitudinal direction at a stretching temperature of 120 to 150°C, and then 1
It is stretched 5 to 15 times in the width direction at a stretching temperature of 50 to 170°C.
以上の様にして延伸された該フィルムは、160〜17
5℃で数秒間熱処理される。この時数%のリラックスを
許しながら熱処理ケると寸法安定性が良好となる。また
、さらに必要に応じ、表面活性化処理、例えばN2.C
O2などの各種ガス下でのコロナ放電処理やプラズマ処
理などをして表面張力をあげておくと、印刷インキの接
着性あるいは蒸着金属との接着性が良好となる。The film stretched in the above manner has a 160 to 17
Heat treated at 5° C. for several seconds. At this time, if the heat treatment is carried out while allowing a few percent of relaxation, dimensional stability will be improved. Furthermore, if necessary, a surface activation treatment such as N2. C
If the surface tension is increased by corona discharge treatment or plasma treatment under various gases such as O2, the adhesion of printing ink or adhesion to vapor-deposited metal will be improved.
また、本発明フィルムの表面に易接着性の樹脂、例えば
、エチレン−プロピレンランダム共重合体。Further, a resin easily adhesive to the surface of the film of the present invention, such as an ethylene-propylene random copolymer.
エチレン・エチル・アクリレート共重合体、エチレン・
酢酸ビニル共重合体、アイオノマー等の樹脂をインライ
ンまたはオフラインにて両面または片面にラミネートし
てもよい。Ethylene/ethyl acrylate copolymer, ethylene/
A resin such as a vinyl acetate copolymer or an ionomer may be laminated on both sides or one side in-line or offline.
上記方法によって1qられた白色ポリオレフィンフィル
ムは、各種印刷用紙、各種ラベル、菓子やスナック等の
包装および装飾用として好適であるばかりか、粘着テー
プ用ベースフィルムとしても良好な特性を有する。The white polyolefin film obtained by the above method is not only suitable for various printing papers, various labels, wrapping and decoration of confectionery and snacks, but also has good properties as a base film for adhesive tapes.
[発明の効果]
本発明の白色ポリオレフィンフィルムは次のような優れ
た点を有する。[Effects of the Invention] The white polyolefin film of the present invention has the following excellent points.
(1) 白く、隠蔽性に優れ、フィルム表面の光沢度
が高くて印刷性に優れると共に、二次加工工程で必要な
機械強度、耐寸法安定性、耐溶剤性を有している。(1) It is white, has excellent hiding properties, has a high gloss on the film surface and has excellent printability, and has the mechanical strength, dimensional stability, and solvent resistance necessary for secondary processing steps.
(2) 実質的に無機フィラーを含まないため内部ボ
イドが微小であり、菓子等の包装用として必要な防湿性
に優れている。(2) Since it contains virtually no inorganic filler, internal voids are small and it has excellent moisture resistance, which is necessary for packaging confectionery and the like.
(3)製膜性、コスト性に優れている。(3) Excellent film formability and cost efficiency.
[測定法]
次に、本発明における各特性値の測定法及び用語につい
て以下まとめて示す。[Measurement method] Next, the measurement method and terminology of each characteristic value in the present invention will be summarized below.
(1) 極限粘度([η])
試料0.1gを135℃のテトラリン100dに完全溶
解させ、この溶液を粘度計で135℃の恒温槽中で測定
して比粘度Sより次式に従って極限粘度を求める。(1) Intrinsic viscosity ([η]) Completely dissolve 0.1 g of sample in 100 d of tetralin at 135°C, measure this solution with a viscometer in a constant temperature bath at 135°C, and calculate the intrinsic viscosity from the specific viscosity S according to the following formula. seek.
単位はdl/l;lとする。The unit is dl/l;l.
[η]=S10.1X (1+0.22xS)(2)
アイソタクチックインデックス(I l)あるいはn
−ヘプタン抽出残分
試料を130℃で2時間真空乾燥する。これから重量W
(#Ig>の試料をとり、ソックスレー抽出器に入れ沸
l1n−ヘプタンで12時間抽出する。[η]=S10.1X (1+0.22xS) (2)
Isotactic index (I l) or n
- Vacuum dry the heptane extraction residue sample at 130°C for 2 hours. From now on weight W
(Take a sample of #Ig>, put it in a Soxhlet extractor, and extract with boiling l1n-heptane for 12 hours.
次に、この試料を取出しアセトンで十分洗浄したのち、
130℃で6時間真空乾燥しその後、重量w−<ms>
を測定し、次式で求める。Next, take out this sample and wash it thoroughly with acetone.
After vacuum drying at 130°C for 6 hours, the weight w-<ms>
is measured and calculated using the following formula.
II(%)=W′/Wx100 (3) 破断強度 JIS K−6782に準する。II (%) = W'/Wx100 (3) Breaking strength Conforms to JIS K-6782.
(4) ヤング率 ASTM D−882−75bに準する。(4) Young's modulus Conforms to ASTM D-882-75b.
(5)融解温度(Tm)・溶融結晶化温度(TIIIC
)試料5ηを走査型熱量計DSC−II型(Perki
r)E1mer社製)にセットし、窒素気流下で昇温速
度20℃/分にて室温より測定し、融解に伴う吸熱ピー
ク温度を融解温度Tmとする。(5) Melting temperature (Tm)/melt crystallization temperature (TIIIC
) Sample 5η was measured using a scanning calorimeter DSC-II model (Perki
r) manufactured by Elmer Co., Ltd., and measured from room temperature under a nitrogen stream at a heating rate of 20° C./min, and the endothermic peak temperature accompanying melting is defined as the melting temperature Tm.
また、同様にして試料を280℃にて5分間保った後に
、降温速度20℃/分にて室温まで温度を下げていった
時に、結晶化に伴う放熱ピーク温度を溶融結晶化温度T
mcとする。Similarly, after keeping the sample at 280°C for 5 minutes, the temperature was lowered to room temperature at a cooling rate of 20°C/min.
Let it be mc.
(6) メルトフローインデックス(Ml)ASTM
−D−1238にて、260℃、5Ksの条件で測定す
る。(6) Melt flow index (Ml) ASTM
-D-1238, measured at 260°C and 5Ks.
単位はg/10分で表わす。The unit is g/10 minutes.
(7) 光学濃度(OD) マクベス社濃度計モデルTD504で測定する。(7) Optical density (OD) Measurement is performed using a Macbeth densitometer model TD504.
透過濃度をD、入射光量をIo、透過光量をIとすると
、
D=−1op (I/Io ) で定義される。When the transmitted density is D, the amount of incident light is Io, and the amount of transmitted light is I, it is defined as D=-1op (I/Io).
(8) 光沢度
JIS−Z8741 (60” −60” ’)に準す
る。(8) Glossiness According to JIS-Z8741 (60"-60"').
(9) 隠蔽性
フィルムの隠蔽性とは不透明度を示すものであり、AS
TM−Dl 003−52法に準じ測定したベイズが9
0%以上を○、89〜80%の範囲を△、80%以下を
×とした。(9) Hiding ability of a hiding film indicates opacity, and AS
Bayesian measured according to TM-Dl 003-52 method is 9
0% or more was rated as ◯, 89-80% was rated as △, and 80% or less was rated as ×.
(10)印刷性
フィルムの表面にコロナ放電処理を行ない、その処理面
に市販セロファン用印刷インキセロカラーST r白」
(東洋インキ製造■製)をコーティングバー#5にて
塗布し、80℃オーブンで1分間乾燥した後、25℃、
50%RH下に24時間放置した。(10) The surface of the printable film is subjected to corona discharge treatment, and the treated surface is coated with commercially available cellophane printing ink Cellocolor STr White.
(manufactured by Toyo Ink Manufacturing ■) using Coating Bar #5, dried in an oven at 80℃ for 1 minute, and then heated at 25℃.
It was left under 50% RH for 24 hours.
a、セロテープ剥離テスト
印刷フィルムにセロテープ(槽水化学■製NQ1150
、幅24#l111)を貼付して強く引剥し、インキ剥
離面積により次の通り5段階評価した。a. Sellotape peel test
, width 24#l111) was attached and strongly peeled off, and the ink peeled area was evaluated in the following five grades.
インキ剥離面積O% 二判定5インキ剥
離面積10%未満 二判定4インキ剥離面積1
0%以上25%未満:判定3インキ剥離面積25%以上
50%未満二判定2インキ剥離面積50%以上
:判定1b、印刷加工テスト
フィルム1000mをグラビア印刷した時に、インキの
にじみ、印字のずれ、フィルムのシワ等のトラブル発生
の有無を評価した。Ink peeling area O% 2nd judgment 5 Ink peeling area less than 10% 2nd judgment 4 Ink peeling area 1
0% or more and less than 25%: Judgment 3 Ink peeled area 25% or more and less than 50% 2 Judgment 2 Ink peeled area 50% or more
: Judgment 1b, printing processing test When 1000 m of film was gravure printed, the presence or absence of troubles such as ink bleeding, misalignment of print, and wrinkles of the film was evaluated.
01)打扱き加工テスト
フィルムを100枚/分の速度でラベルの打抜きテスト
を行ない、打抜き不良やシワおよびよじれ等の不良個数
を評価した。01) Punching test The film was subjected to a label punching test at a speed of 100 sheets/minute, and the number of defects such as punching defects, wrinkles, and kinks was evaluated.
(財)密度 JIS−に6758に準する。Density Conforms to JIS-6758.
[実施例] 以下、本発明を実施例に基づいて説明する。[Example] Hereinafter, the present invention will be explained based on examples.
実施例1
[η]が1.85d110、II=97%のポリプロピ
レンホモポリマー(三井東圧化学■製“三井ノーブレン
” FO−850)100重間部と、メチルペンテンホ
モポリマー(三井石油化学■製”TPX”MX−019
、n−ヘプタン抽出残分=95%、MI=1009/1
0分)12重量部をヘンシェルミキサーで混合後、30
mφの二軸押出機にて280℃で溶融押出してペレット
を作成した。該ペレットを35Mφの一軸押出機に供給
し、T−ダイにて290℃の樹脂温度でシート状に押出
し、60℃に保たれた冷却ドラム上で固化し、厚ざ80
0℃1mのポリオレフィン組成物シートを得た。該シー
トをロール式縦延伸機にて110℃で縦方向に弾性限界
内の倍率1.15倍の微延伸をし、さらに縦方向に13
5℃で4.5倍延伸した(多、引続きステンターに導き
横方向に160℃にて8倍に延伸し、5%のリラックス
を許しつつ165℃にて熱処理し、厚さ20μmの二軸
配向ポリオレフィンフィルムを得た。(第1表参照)。Example 1 A polypropylene homopolymer with [η] of 1.85d110 and II=97% (“Mitsui Noblen” FO-850 manufactured by Mitsui Toatsu Chemicals) and a methylpentene homopolymer (manufactured by Mitsui Petrochemicals) "TPX" MX-019
, n-heptane extraction residue=95%, MI=1009/1
0 minutes) After mixing 12 parts by weight with a Henschel mixer, 30 parts by weight
Pellets were prepared by melt extrusion at 280° C. using a mφ twin-screw extruder. The pellets were fed into a 35 Mφ single screw extruder, extruded into a sheet using a T-die at a resin temperature of 290°C, solidified on a cooling drum kept at 60°C, and made into a sheet with a thickness of 80°C.
A polyolefin composition sheet having a temperature of 1 m at 0°C was obtained. The sheet was slightly stretched in the longitudinal direction at 110°C with a roll-type longitudinal stretching machine at a magnification of 1.15 times within the elastic limit, and further stretched in the longitudinal direction by 1.15 times.
Stretched 4.5 times at 5°C (multiple, then passed through a stenter and stretched 8 times in the transverse direction at 160°C, heat treated at 165°C while allowing 5% relaxation, biaxially oriented with a thickness of 20 μm) A polyolefin film was obtained (see Table 1).
該フィルムの光学特性を調べたところ、光学濃度(OD
)が0.3であり、光沢度はドラム面89%、非ドラム
面88%であり、ベイズは97%で白くて隠蔽性に優れ
た特性を有していることが分かる。When the optical properties of the film were investigated, the optical density (OD
) is 0.3, the glossiness is 89% on the drum surface and 88% on the non-drum surface, and the baize is 97%, indicating that it is white and has excellent hiding properties.
また該フィルムの機械特性を調べたところ、長手方向の
強度が12Kg/mTdであり、長手方向と幅方向のヤ
ング率の和は520Kg/mmであった。Further, when the mechanical properties of the film were examined, the strength in the longitudinal direction was 12 Kg/mTd, and the sum of the Young's modulus in the longitudinal direction and the width direction was 520 Kg/mm.
さらに、該フィルムは印刷性に優れていることが分かる
。(第2表参照)。Furthermore, it can be seen that the film has excellent printability. (See Table 2).
比較例1
実施例1と同様にして得たポリオレフィン組成物シート
を従来の逐次二軸延伸法で縦方向に135℃で一挙5倍
延伸後、ステンターにて横方向に160℃で8倍延伸し
て厚さ20μmの二軸配向ポリオレフィンフィルムを1
qだ。該フィルムは、光学濃度(OD)が0.08で、
ヘイズは68%と白さ、隠蔽性に劣っていた。(第1,
2表参照)実施例2
[η]が2.25dl/g、II=97%のポリプロピ
レンホモポリマー(三井東圧化学側製“三井ノー7レン
” JS−1429)100重量部と、メチルペンテン
コポリマー(三井石油化学■製゛TPX”RT−18、
n−ヘプタン抽出残分=74%、MI=269/10分
)18重組部を混合後、実施例1と同様にして押出し固
化し、厚さ600μmのポリオレフィン組成物シートを
得た。該シ−トをロール式縦延伸機にて100’Cで縦
方向に弾性限界内の倍率1.20倍の微延伸した後、ス
テンター式同時延伸機にて165℃で縦横延伸共に5倍
に同時延伸し、厚さ20μmのフィルムを得た。(第1
表参照)。Comparative Example 1 A polyolefin composition sheet obtained in the same manner as in Example 1 was stretched 5 times in the machine direction at 135° C. by a conventional sequential biaxial stretching method, and then stretched 8 times in the transverse direction at 160° C. using a stenter. A biaxially oriented polyolefin film with a thickness of 20 μm was
It's q. The film has an optical density (OD) of 0.08,
The haze was 68%, which was poor in whiteness and concealment. (First,
(See Table 2) Example 2 100 parts by weight of polypropylene homopolymer with [η] of 2.25 dl/g and II = 97% (“Mitsui No7ren” JS-1429 manufactured by Mitsui Toatsu Chemical Co., Ltd.) and methylpentene copolymer. (Mitsui Petrochemical ■TPX”RT-18,
n-heptane extraction residue = 74%, MI = 269/10 minutes) After mixing 18 folds, extrusion and solidification were performed in the same manner as in Example 1 to obtain a polyolefin composition sheet with a thickness of 600 μm. The sheet was slightly stretched in the machine direction at 100'C using a roll type longitudinal stretching machine at a magnification of 1.20 times within the elastic limit, and then stretched to 5 times both length and width at 165°C using a stenter type simultaneous stretching machine. This was simultaneously stretched to obtain a film with a thickness of 20 μm. (1st
(see table).
該フィルムの光学濃度(OD)は0.2であり、光沢度
はドラム面75%、非ドラム面72%であり、ヘイズは
92%と白さ、隠蔽性に優れていた。The optical density (OD) of the film was 0.2, the gloss was 75% on the drum side and 72% on the non-drum side, and the haze was 92%, indicating excellent whiteness and hiding properties.
また、長手方向の強度は1QKg/mrtt、長手方向
と幅方向のヤング率の和は350Kg/mmであった。Further, the strength in the longitudinal direction was 1QKg/mrtt, and the sum of the Young's modulus in the longitudinal direction and the width direction was 350Kg/mm.
(第2表参照)。(See Table 2).
比較例2
ポリプロピレンホモポリマー(FO−850>100重
量部とメチルペンテンホモポリマー(MX−019>6
0重量部の組成物を実施例1と同様に製膜しようとした
が、製膜性が極めて不安定なため、微延伸温度を130
℃、縦延伸温度を140℃、横延伸温度を172℃とし
て厚さ22μmのフィルムを得た。(第1表参照)。該
フィルムは内部ボイドが多く光学濃度(OD)は0.2
と高いが、光沢度は37%と低く、長手方向の強度は6
に9/mrd、長手方向と幅方向のヤング率の和は23
0に’j/mrdと小さく、印刷加工時にフィルム端部
がたるみ、印字のずれが発生した。(第2表参照)。Comparative Example 2 Polypropylene homopolymer (FO-850>100 parts by weight and methylpentene homopolymer (MX-019>6)
An attempt was made to form a film using 0 parts by weight of the composition in the same manner as in Example 1, but the film forming properties were extremely unstable, so the slight stretching temperature was changed to 130 parts by weight.
℃, the longitudinal stretching temperature was 140°C, and the transverse stretching temperature was 172°C to obtain a film with a thickness of 22 μm. (See Table 1). The film has many internal voids and has an optical density (OD) of 0.2.
However, the gloss level is low at 37%, and the longitudinal strength is 6.
9/mrd, the sum of the Young's modulus in the longitudinal direction and the width direction is 23
It was as small as 0'j/mrd, and the edge of the film sagged during printing, causing misalignment of the print. (See Table 2).
比較例3
ポリプロピレンホモポリマー(JS−1429>100
重間部と炭酸カルシウム25重量部の組成物を実施例1
と同様にして厚さ30μmのフィルムを得た。(第1表
参照)該フィルムは光学yA度(OD)およびヘイズが
高く、白さ、隠蔽性に優れるものの、ボイド容積が大き
いため、光沢度、機械特性に劣ることが分かる。(第2
表参照)。Comparative Example 3 Polypropylene homopolymer (JS-1429>100
Example 1 A composition containing 25 parts by weight of interstitial part and calcium carbonate
A film with a thickness of 30 μm was obtained in the same manner as above. (See Table 1) Although the film has a high optical yA degree (OD) and haze, and is excellent in whiteness and hiding properties, it is found that the glossiness and mechanical properties are poor because of the large void volume. (Second
(see table).
Claims (2)
以上のポリオレフィンフィルムであって、該フィルムの
長手方向の強度が8Kg/m_m^2以上で、長手方向
と幅方向のヤング率の和が250Kg/m_m^2以上
であることを特徴とする白色ポリオレフィンフィルム。(1) Optical density (OD) is 0.1 or more, gloss is 40%
A white polyolefin film as described above, characterized in that the strength in the longitudinal direction of the film is 8 Kg/m_m^2 or more, and the sum of the Young's modulus in the longitudinal direction and the width direction is 250 Kg/m_m^2 or more. film.
以上、極限粘度が1.2〜3.5dl/gのポリプロピ
レン100重量部に、n−ヘプタン抽出残分が40%以
上であるメチルペンチッポリマーを5〜50重量部添加
してなる樹脂をシート状またはチューブ状に溶融成形後
、120℃以下の温度で、弾性限界内での微延伸をした
後、さらに120℃〜170℃の温度ですくなくとも一
軸に延伸することを特徴とする白色ポリオレフィンフィ
ルムの製造方法。(2) Isotactic index (II) is 80%
As described above, a sheet of resin is prepared by adding 5 to 50 parts by weight of methyl pentyl polymer having an n-heptane extraction residue of 40% or more to 100 parts by weight of polypropylene having an intrinsic viscosity of 1.2 to 3.5 dl/g. A white polyolefin film, which is melt-formed into a shape or a tube, subjected to slight stretching within the elastic limit at a temperature of 120°C or lower, and further stretched at least uniaxially at a temperature of 120°C to 170°C. Production method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63294299A JP2611392B2 (en) | 1988-11-21 | 1988-11-21 | White polyolefin film and method for producing the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63294299A JP2611392B2 (en) | 1988-11-21 | 1988-11-21 | White polyolefin film and method for producing the same |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02139220A true JPH02139220A (en) | 1990-05-29 |
JP2611392B2 JP2611392B2 (en) | 1997-05-21 |
Family
ID=17805900
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63294299A Expired - Fee Related JP2611392B2 (en) | 1988-11-21 | 1988-11-21 | White polyolefin film and method for producing the same |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2611392B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014084324A (en) * | 2012-10-19 | 2014-05-12 | Mitsubishi Plastics Inc | Polypropylene-based resin porous film |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8491991B2 (en) | 2004-04-22 | 2013-07-23 | Toray Industries, Inc. | Microporous polypropylene film and process for producing the same |
JP7484122B2 (en) * | 2019-10-11 | 2024-05-16 | Toppanホールディングス株式会社 | White sheet, decorative sheet and manufacturing method thereof |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5133153A (en) * | 1974-09-13 | 1976-03-22 | Kishimoto Sangyo Co | KOTSUPU YOKITO NO SEIZOHOHO |
-
1988
- 1988-11-21 JP JP63294299A patent/JP2611392B2/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5133153A (en) * | 1974-09-13 | 1976-03-22 | Kishimoto Sangyo Co | KOTSUPU YOKITO NO SEIZOHOHO |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014084324A (en) * | 2012-10-19 | 2014-05-12 | Mitsubishi Plastics Inc | Polypropylene-based resin porous film |
Also Published As
Publication number | Publication date |
---|---|
JP2611392B2 (en) | 1997-05-21 |
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