JPS6132139B2 - - Google Patents

Info

Publication number
JPS6132139B2
JPS6132139B2 JP52127075A JP12707577A JPS6132139B2 JP S6132139 B2 JPS6132139 B2 JP S6132139B2 JP 52127075 A JP52127075 A JP 52127075A JP 12707577 A JP12707577 A JP 12707577A JP S6132139 B2 JPS6132139 B2 JP S6132139B2
Authority
JP
Japan
Prior art keywords
film
layer
polypropylene
laminated
thickness
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
Application number
JP52127075A
Other languages
Japanese (ja)
Other versions
JPS5460370A (en
Inventor
Kunio Kondo
Tatsuhiko Futaboshi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Gunze Ltd
Original Assignee
Gunze Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Gunze Ltd filed Critical Gunze Ltd
Priority to JP12707577A priority Critical patent/JPS5460370A/en
Publication of JPS5460370A publication Critical patent/JPS5460370A/en
Publication of JPS6132139B2 publication Critical patent/JPS6132139B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明はカール現象の少ない、腰の良好な透
明、ハイガスバリヤー性積層フイルムの製造法に
関する。 従来、ガスバリヤー性の良好な複合フイルムと
して特定のエチレン−酢酸ビニル共重合体(以下
「けん化物」と略称する)と変性ポリオレフイン
とポリプロピレンの三層からなり、かつポリプロ
ピレン層が2軸に他の2層が1軸延伸されたもの
例えば特開昭52−54784号等が知られている。し
かしながらこの種の複合フイルムはけん化物の吸
湿性のためけん化物層からポリプロピレン層にカ
ールするという欠点を有していた。そしてこのカ
ール現象はけん化物層や変性ポリオレフイン層が
一軸に延伸されていることと相和して尚、助長さ
れる傾向にあつた。また変性ポリプロピレン層の
厚さは実用的速度である20〜100m/minにおいて
工業生産される場合、0.8μ以下にするとは極め
て困難であり、このため複合フイルムの透明性を
阻害する原因となつている上に本来良好なポリプ
ロピレンの腰をも阻害していた。何故ならば一般
に変性ポリプロピレンはダイスから溶融押出され
る時の厚さは12〜15μが限界であり、一方けん化
物は前記実用的速度において15倍以上に延伸する
ことは極めて困難であるため、変性ポリプロピレ
ンがけん化物と共に1軸延伸されても0.8μ以下
の厚さとはなり得ず前記の如き欠点を是正するこ
とができなかつた。 ここにおいて本発明者らは上記欠点を改良すべ
く鋭意研究の結果遂に、カール現象の少ない腰、
透明の良好なガスバリヤー性積層フイルムの製造
法を供給することに成功した。即ち本発明はポリ
プロピレンと接着性ポリオレフイン系樹脂とを共
押出積層するか又は、ポリプロピレンフイルムに
接着性ポリオレフイン系樹脂を溶融押出積層して
なる二層フイルムを経方向に2〜12倍延伸し、次
いで斯る2層フイルムの前記接着性ポリオレフイ
ン系樹脂面に更にエチレン含有量25〜60モル%、
けん化度90%以上のエチレン−酢酸ビニル共重合
体けん化物を溶融押出積層し、しかる後違方向に
5〜15倍に延伸したことを特徴とする積層フイル
ムの製造法に係るものである。 本発明に係るポリプロピレンとはポリプロピレ
ン及びこれとエチレン等他のα−オレフインとの
共重合体であり、特に結晶性のポリプロピレンが
好ましい。 またけん化物とはエチレン含有量25〜60モル
%、好ましくは30〜50モル%、けん化度90%以
上、好ましくは95%以上のものでありこの範囲を
はづれるものは本発明には不適である。更に接着
性ポリオレフイン系樹脂とはポリエチレン、ポリ
プロピレン、又はこれらの共重合体又はこれらと
他のα−オレフインや酢酸ビニルなどとの共重合
体等のポリオレフインにアクリル酸、マレイン
酸、フマル酸などの不飽和カルボン酸またはその
酸無水物、エステル等の誘導体から選ばれた少な
くとも1種を10-4〜10重量%、好ましくは10-3
5重量%の範囲でグラフト共重合させてある変性
ポリオレフインを含有する樹脂であり、このもの
は変性ポリオレフインのみで構成されていても良
く、また変性ポリオレフインに未変性ポリオレフ
イン及び/又は第三者を混合したものでもよい。
特に好ましい例としてはポリプロピレン、エチレ
ン−プロピレン共重合体等に無水マレイン酸をグ
ラフト共重合させてなる高融点のものが本発明の
効果をもつとも良好に発揮できる。 本発明に係る延伸倍率としては経方向2〜12倍
好ましくは3〜7倍であり、緯方向に5〜15倍好
ましくは7〜12倍であり、この範囲以外ではフイ
ルムの破損が生じたり物性面で好ましくない現象
を生ずるので使用に耐えない。また延伸温度は経
方向90〜160℃、緯方向130〜190℃、好ましくは
経方向110〜140℃、緯方向140〜170℃の範囲で行
うのがよく特に経方向は接着性ポリオレフイン系
樹脂が溶融して、延伸ロール等に付着しない範囲
で行なうのが好ましい。更に緯方向の延伸につい
てはテンター方式で行うのが好ましく、その延伸
速度としては20〜100m/min好ましくは50〜80
m/minで行う必要があり、これ以下の値では生
産性が低下し、これ以上では延伸不適となり好ま
しくない。 本発明に係る製造法においては「けん化物」を
経延伸された二層フイルムに溶融押出積層するこ
とが最も望ましい。この他に「けん化物」を押出
してフイルム化した状態で連続的に前記二層フイ
ルムに積層することも当然本願に係る「溶融押出
積層」の範囲に属するものである。またこのこと
は本発明に係るポリプロピレンフイルムに接着性
ポリオレフイン系樹脂を溶融押出積層する際も当
然云い得ることである。接着性ポリオレフイン層
の厚さとしては0.8〜0.1μ、好ましくは0.2〜0.5
μであり、0.8μ以上では透明性を阻害し0.1μ以
下では接着性が乏しくなる。一般にこの値は前記
延伸速度で生産される通常のガスバリヤー性積層
フイルムでは至難の値であり、本発明に限りこの
値は十分保証されるものである。 尚、この厚さについては本発明の如き、値を取
ることにより次の如き効果も期待できる。即ち一
般に積層フイルムは積層物(被覆物)の厚さが薄
い程、延伸中に生ずる厚みのバラツキが少なくな
るため緯延伸にテンター方式を応用する際クリツ
プ際までラミネートせず、第1図の如き状態で積
層しクリツプがポリプロピレン層1の耳部のみを
挾持したとしても、適宜に均一な厚さの延伸が可
能であり、延伸後の積層際の状態も第2図に示す
如く良好でかつ厚さも均一であつた。そしてこの
ようにすることにより後刻耳部を回収する場合ポ
リプロピレン層のみからなるクリツプ挾持跡を有
する耳部を第2図鎖線4にそつて回収すればよい
ことになり屑回収に対しても極めて効果的であ
る。一方従来のものは変性ポリオレフイン層を薄
くできないため、クリツプ際まで積層せず上記の
如く例えポリプロピレン層のみをクリツプにかけ
て延伸したとしても、その引張り応力の影響のた
め積層際の状態が第3図に示す如く凸凹となり厚
み精度がでにくく、耳部を回収する際ポリプロピ
レン層のみを回収することは不可能で第3図鎖線
4に示す如く変性ポリオレフイン層、更には「け
ん化物層」の三層からなる積層際の部分まで除去
する必要があつた。そしてこの耳部回収物は三者
が混りかつ強固にくつついているため相溶性に欠
け、透明性に欠如しているためその利用価値を見
出すのに苦慮していたが本発明によるとこれらの
欠点も一挙に解決できる等の格別なる有用をも奏
するものである。 本発明は以上の如くであり、本発明の製造法に
よるガスバリヤー性積層フイルムはカール現象が
生じにくいので、包装フイルムとして応用する時
特にその製袋性、包装適性に優れ自動機に適応す
る際効果的である。更に透明度が高く腰が良好な
ので一般包装から特殊包装に至るまでその適応範
囲は極めて広く、かつヒートシール強度も十分で
層間剥離の生ずることもない等の格別な効果を奏
するものである。本発明に係る積層フイルムは特
にガスバリアー性、ヒートシール性が良好なので
一般包装や生鮮食料品等の特殊包装等に好適であ
るが、勿論その他適宜の用途に応用でき得るもの
である。 次に本発明の実施例を述べる。 実施例 1 結晶性ポリプロピレンの押出フイルム(厚さ
1060μ)に、ポリプロピレンに無水マレイン酸
3.5重量%グラフト共重合させたもの5部とポリ
プロピレン95部との混合体からなる接着性ポリオ
レフイン系樹脂(融点160℃)を厚さ40μで溶融
押出ラミネートし次いで約130℃において経方向
に5倍に延伸し1軸延伸二層フイルムを得た。斯
る二層フイルムの接着性ポリオレフイン層に更に
30μのエチレン含有量40モル%、けん化度98%の
エチレン−酢酸ビニル共重合体けん化物を溶融押
出しラミネートししかる後50m/minの速度で160
℃にて緯方向に10倍に延伸し、積層フイルムを得
た。このフイルムの厚さは25μでこのうち接着性
ポリオレフイン層の厚さは0.8μであつた。 実施例 2 実施例1と同様の方法で接着性ポリオレフイン
層のみ0.2μとなるような構成として積層フイル
ムを得た。 比較例 1 実施例1と同様の樹脂により厚さ205μの一軸
延伸ポリプロピレンフイルムに厚さ15μの接着性
ポリオレフイン系樹脂と厚さ30μのけん化物とを
遂時溶融押出ラミネートし、しかる後実施例1と
同様の方法で緯方向に延伸し、接着性ポリオレフ
イン層の厚さが1.5μの積層フイルムを得た。他
の2層の厚さは実施例1と同様であつた。 比較例 2 比較例1と同様の方法で8μの接着性ポリオレ
フインフイルムを溶融押出ラミネートしようとし
たが押出製膜はできなかつた。 比較例 3 比較例1と同様の方法で緯方向の延伸倍率を16
倍とした所「けん化物」層にクラツクが入り良好
なフイルムを得ることができなかつた。 比較例 4 実施例1と同様の樹脂を用い3台の押出機より
一つのダイスに導き、三層共押出フイルムを得、
しかる後実施例1と同様の延伸条件にて経緯に2
軸延伸した所、「けん化物」層にクラツクを入り
良好なフイルムが得られなかつた。 以上の実施例、比較例から明らかな通り、接着
性ポリオレフインは12μ以下に押出製膜すること
は困難であり、一方「けん化物」は15倍以上に延
伸することが困難なため、従来の方向では接着性
ポリオレフイン層を0.8μ以下とすることは不可
能であることが解かる。これに対し本発明のもの
は0.2μのものも可能でありその物性についても
第1表に示す通り従来のものに比して格別顕著な
効果がある。
The present invention relates to a method for producing a transparent, high gas barrier laminated film with little curling and good elasticity. Conventionally, a composite film with good gas barrier properties consists of three layers: a specific ethylene-vinyl acetate copolymer (hereinafter referred to as "saponified material"), a modified polyolefin, and polypropylene, and the polypropylene layer is biaxially connected to other layers. For example, JP-A No. 52-54784 is known, in which two layers are uniaxially stretched. However, this type of composite film had the disadvantage of curling from the saponified layer to the polypropylene layer due to the hygroscopic nature of the saponified material. This curling phenomenon tended to be promoted in harmony with the fact that the saponified layer and modified polyolefin layer were uniaxially stretched. Furthermore, it is extremely difficult to reduce the thickness of the modified polypropylene layer to 0.8 μ or less when industrially produced at practical speeds of 20 to 100 m/min, which may impede the transparency of the composite film. Moreover, it was also inhibiting the elasticity of polypropylene, which is originally good. This is because modified polypropylene generally has a maximum thickness of 12 to 15μ when melt extruded from a die, while it is extremely difficult to stretch saponified polypropylene more than 15 times at the above-mentioned practical speed. Even if polypropylene was uniaxially stretched together with a saponified material, the thickness could not be less than 0.8 μm, and the above-mentioned defects could not be corrected. As a result of intensive research to improve the above-mentioned drawbacks, the present inventors have finally found a waist with less curling phenomenon.
We have succeeded in providing a method for producing a transparent laminated film with good gas barrier properties. That is, in the present invention, a two-layer film obtained by co-extrusion laminating polypropylene and an adhesive polyolefin resin, or by melt-extruding laminating an adhesive polyolefin resin on a polypropylene film, is stretched 2 to 12 times in the warp direction, and then Further, on the adhesive polyolefin resin surface of the two-layer film, an ethylene content of 25 to 60 mol%,
This invention relates to a method for producing a laminated film, characterized in that saponified ethylene-vinyl acetate copolymers having a saponification degree of 90% or more are laminated by melt extrusion and then stretched 5 to 15 times in the opposite direction. The polypropylene according to the present invention refers to polypropylene and a copolymer of this and other α-olefins such as ethylene, and crystalline polypropylene is particularly preferred. In addition, saponified products have an ethylene content of 25 to 60 mol%, preferably 30 to 50 mol%, and a degree of saponification of 90% or more, preferably 95% or more, and those that fall outside this range are unsuitable for the present invention. It is. Furthermore, adhesive polyolefin resins are polyolefins such as polyethylene, polypropylene, copolymers thereof, or copolymers of these with other α-olefins, vinyl acetate, etc., and inorganic compounds such as acrylic acid, maleic acid, and fumaric acid. At least one selected from saturated carboxylic acids or their derivatives such as acid anhydrides and esters in an amount of 10 -4 to 10% by weight, preferably 10 -3 to
This is a resin containing a modified polyolefin that has been graft copolymerized in a range of 5% by weight, and may be composed only of the modified polyolefin, or a modified polyolefin mixed with an unmodified polyolefin and/or a third party. It may be something you have done.
Particularly preferred examples include polypropylene, ethylene-propylene copolymers, etc., which have a high melting point and are made by graft copolymerizing maleic anhydride, and can exhibit the effects of the present invention well. The stretching ratio according to the present invention is 2 to 12 times in the warp direction, preferably 3 to 7 times, and 5 to 15 times in the weft direction, preferably 7 to 12 times. It is not usable because it causes undesirable phenomena on the surface. The stretching temperature is preferably 90 to 160°C in the warp direction and 130 to 190°C in the weft direction, preferably 110 to 140°C in the warp direction and 140 to 170°C in the weft direction. It is preferable to carry out the process to the extent that it is melted and does not adhere to stretching rolls or the like. Furthermore, stretching in the weft direction is preferably carried out by a tenter method, and the stretching speed is 20 to 100 m/min, preferably 50 to 80 m/min.
It is necessary to carry out the stretching at m/min. If the value is less than this, the productivity will decrease, and if it is more than this, it will become unsuitable for stretching, which is not preferable. In the production method according to the present invention, it is most desirable to melt-extrude and laminate the "saponified material" onto a warp-stretched two-layer film. In addition, it goes without saying that the extrusion of a saponified material into a film and its continuous lamination on the two-layer film also falls within the scope of the "melt extrusion lamination" according to the present application. Naturally, this also applies when melt-extrusion laminating an adhesive polyolefin resin to the polypropylene film according to the present invention. The thickness of the adhesive polyolefin layer is 0.8 to 0.1 μ, preferably 0.2 to 0.5
If it is 0.8μ or more, transparency will be impaired, and if it is 0.1μ or less, adhesiveness will be poor. Generally, this value is extremely difficult to achieve for ordinary gas barrier laminated films produced at the above-mentioned drawing speed, and this value is fully guaranteed only in the present invention. Incidentally, by taking a value for this thickness as in the present invention, the following effects can be expected. In other words, in general, the thinner the laminated film (coating) is, the less variation in thickness that occurs during stretching. Even if the clips hold only the edges of the polypropylene layer 1, it is possible to stretch the polypropylene layer 1 to a uniform thickness, and the lamination state after stretching is also good and thick, as shown in Figure 2. It was also uniform. By doing this, when collecting the ears later, it is only necessary to collect the ears having the clip retaining marks made of only the polypropylene layer along the chain line 4 in Figure 2, which is extremely effective for collecting waste. It is true. On the other hand, in the conventional method, the modified polyolefin layer cannot be thinned, so even if only the polypropylene layer is stretched by clipping as described above, the state at the time of lamination is as shown in Figure 3 due to the effect of the tensile stress. As shown in Fig. 3, the unevenness makes it difficult to obtain thickness accuracy, and it is impossible to collect only the polypropylene layer when collecting the ears. It was necessary to remove even the parts where the layers were stacked. Since the recovered ear part is a mixture of three substances and is tightly attached, it lacks compatibility and lacks transparency, so it has been difficult to find its useful value. However, according to the present invention, these It is also extremely useful, such as being able to solve shortcomings all at once. The present invention is as described above, and since the gas barrier laminated film produced by the production method of the present invention is less prone to curling, it has excellent bag-making properties and packaging suitability especially when applied as a packaging film, and is suitable for automatic machines. Effective. Furthermore, it has high transparency and good elasticity, so it has an extremely wide range of applications ranging from general packaging to special packaging, and has special effects such as sufficient heat sealing strength and no delamination. The laminated film according to the present invention has particularly good gas barrier properties and heat sealability, so it is suitable for general packaging and special packaging for fresh foods, etc., but it can of course be applied to other appropriate uses. Next, examples of the present invention will be described. Example 1 Extruded crystalline polypropylene film (thickness
1060μ), maleic anhydride to polypropylene
An adhesive polyolefin resin (melting point: 160°C) consisting of a mixture of 5 parts of 3.5% by weight graft copolymer and 95 parts of polypropylene is melt-extruded and laminated to a thickness of 40μ, and then laminated by 5 times in the warp direction at approximately 130°C. A uniaxially stretched two-layer film was obtained. In addition to the adhesive polyolefin layer of such a two-layer film,
A saponified ethylene-vinyl acetate copolymer with a 30μ ethylene content of 40 mol% and a saponification degree of 98% was melt-extruded and laminated, and then heated at a speed of 50 m/min to 160 m/min.
The film was stretched 10 times in the latitudinal direction at ℃ to obtain a laminated film. The thickness of this film was 25μ, of which the thickness of the adhesive polyolefin layer was 0.8μ. Example 2 A laminated film was obtained in the same manner as in Example 1 so that only the adhesive polyolefin layer had a thickness of 0.2μ. Comparative Example 1 Using the same resin as in Example 1, a uniaxially stretched polypropylene film with a thickness of 205 μm was melt-extruded and laminated with an adhesive polyolefin resin with a thickness of 15 μm and a saponified material with a thickness of 30 μm. A laminated film with an adhesive polyolefin layer having a thickness of 1.5 μm was obtained by stretching in the weft direction in the same manner as above. The thicknesses of the other two layers were the same as in Example 1. Comparative Example 2 An attempt was made to melt-extrude and laminate an 8μ adhesive polyolefin film using the same method as in Comparative Example 1, but extrusion film formation was not possible. Comparative Example 3 The stretching ratio in the weft direction was set to 16 using the same method as Comparative Example 1.
When the amount was doubled, cracks appeared in the saponified layer, making it impossible to obtain a good film. Comparative Example 4 The same resin as in Example 1 was introduced into one die from three extruders to obtain a three-layer coextruded film,
After that, under the same stretching conditions as in Example 1, 2
When axially stretched, cracks appeared in the saponified layer and a good film could not be obtained. As is clear from the above examples and comparative examples, it is difficult to extrude adhesive polyolefin into a film of 12μ or less, and on the other hand, it is difficult to stretch ``saponified material'' to more than 15 times. It can be seen that it is impossible to reduce the thickness of the adhesive polyolefin layer to 0.8μ or less. On the other hand, the material of the present invention can have a thickness of 0.2μ, and as shown in Table 1, the material of the present invention has particularly remarkable effects compared to the conventional material.

【表】【table】

【表】 実施例 3 実施例1の方法において第1図に示す如く三者
を積層し、テンターにおけるクリツプによりポリ
プロピレン層のみをはさみ緯延伸したところ延伸
後のものは第2図に示す如くその積層際が良好な
状態で耳部をカツトする際ポリプロピレン層のみ
を回収することが可能であつた。 比較例 5 比較例1の方法において第1図に示す如く三者
を積層し、テンターにてクリツプによりポリプロ
ピレン層のみをはさみ緯延伸した所延伸後のもの
は第3図に示す如くその積層際には凸凹が生じて
いた。従つてその耳部をカツトするためには第3
図の鎖線に示す如く三者の接着した部分までカツ
トせねばならず、耳部の再利用に対に種々の問題
点が生じた。
[Table] Example 3 In the method of Example 1, the three materials were laminated as shown in Figure 1, and only the polypropylene layer was clipped in a tenter and stretched in the weft direction. After stretching, the lamination was as shown in Figure 2. It was possible to recover only the polypropylene layer when cutting the ears with good edges. Comparative Example 5 In the method of Comparative Example 1, the three materials were laminated as shown in Fig. 1, and only the polypropylene layer was held in a tenter with clips and then weft-stretched. There were irregularities. Therefore, in order to cut the ears, the third
As shown by the chain line in the figure, it was necessary to cut out the parts where the three parts were glued together, which caused various problems in reusing the ears.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は三者を積層する際の積層際の状態を示
す断面図であり、第2図は延伸後における耳部を
カツトする状態を示す断面図であり、第3図は三
者を積層し、従来の方法で延伸した後における積
層際の状態を示す断面図であり。 1……ポリプロピレン層、2……接着性ポリオ
レフイン系樹脂層、3……「けん化物」層、4…
…耳部のカツト線、5……積層フイルム、6……
テンタークリツプの跡。
Fig. 1 is a sectional view showing the state of lamination when three parts are laminated, Fig. 2 is a sectional view showing the state of cutting the ears after stretching, and Fig. 3 is a sectional view showing the state of laminating the three parts. FIG. 3 is a cross-sectional view showing the state of lamination after stretching by a conventional method. DESCRIPTION OF SYMBOLS 1... Polypropylene layer, 2... Adhesive polyolefin resin layer, 3... "Saponified material" layer, 4...
...Ear cut line, 5...Laminated film, 6...
Traces of tenter clips.

Claims (1)

【特許請求の範囲】[Claims] 1 ポリプロピレンと接着性ポリオレフイン系樹
脂とを共押出積層するか、又はポリプロピレンフ
イルムに接着性ポリオレフイン系樹脂を溶融押出
積層、もしくは押出ししてフイルム化した状態で
積層してなる二層フイルムを経方向に2〜12倍に
延伸し、次いで斯る二層フイルムの前記接着性ポ
リオレフイン系樹脂面に更にエチレン含有量25〜
60モル%けん化度90%以上のエチレン−酢酸ビニ
ル共重合体けん化物を溶融押出積層もしくはフイ
ルム化した状態で積層し、しかる後緯方向に20〜
100m/minの速度で5〜15倍に延伸し接着性ポリ
オレフイン層の厚さを0.1〜0.8μとしたことを特
徴とする積層フイルムの製造法。
1 A two-layer film formed by co-extrusion lamination of polypropylene and adhesive polyolefin resin, or melt extrusion lamination of adhesive polyolefin resin on polypropylene film, or lamination in the form of a film by extrusion, is laminated in the warp direction. Stretched 2 to 12 times, and then coated with an ethylene content of 25 to 25% on the adhesive polyolefin resin surface of the two-layer film.
A saponified ethylene-vinyl acetate copolymer with a saponification degree of 60 mol% or more is laminated by melt extrusion or in the form of a film, and then laminated in the latitudinal direction for 20 to 30 minutes.
A method for producing a laminated film, characterized in that the adhesive polyolefin layer is stretched 5 to 15 times at a speed of 100 m/min to a thickness of 0.1 to 0.8 μm.
JP12707577A 1977-10-22 1977-10-22 Method of making laminated film Granted JPS5460370A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12707577A JPS5460370A (en) 1977-10-22 1977-10-22 Method of making laminated film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12707577A JPS5460370A (en) 1977-10-22 1977-10-22 Method of making laminated film

Publications (2)

Publication Number Publication Date
JPS5460370A JPS5460370A (en) 1979-05-15
JPS6132139B2 true JPS6132139B2 (en) 1986-07-24

Family

ID=14950949

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12707577A Granted JPS5460370A (en) 1977-10-22 1977-10-22 Method of making laminated film

Country Status (1)

Country Link
JP (1) JPS5460370A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0420193Y2 (en) * 1986-08-30 1992-05-08

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57131523A (en) * 1981-02-07 1982-08-14 Gunze Ltd Manufacture of tubular laminated shrinkable film
US4626782A (en) * 1983-09-26 1986-12-02 The Boeing Company Magnetometer operated at a self-resonant frequency by a sense winding

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5254784A (en) * 1975-10-31 1977-05-04 Toray Ind Inc Composite film

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5254784A (en) * 1975-10-31 1977-05-04 Toray Ind Inc Composite film

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0420193Y2 (en) * 1986-08-30 1992-05-08

Also Published As

Publication number Publication date
JPS5460370A (en) 1979-05-15

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