JPH0564096B2 - - Google Patents
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- Publication number
- JPH0564096B2 JPH0564096B2 JP60290177A JP29017785A JPH0564096B2 JP H0564096 B2 JPH0564096 B2 JP H0564096B2 JP 60290177 A JP60290177 A JP 60290177A JP 29017785 A JP29017785 A JP 29017785A JP H0564096 B2 JPH0564096 B2 JP H0564096B2
- Authority
- JP
- Japan
- Prior art keywords
- resin film
- heat
- film
- perforated
- temperature
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- Perforating, Stamping-Out Or Severing By Means Other Than Cutting (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Molding Of Porous Articles (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明の実施により得られる有孔樹脂フイルム
は、つかいすておむつ、生理用ナプキン等の防漏
材、電解隔膜、構築物の外駆体と内装材との間に
介在させる防湿膜として有用である。
〔従来技術〕
生理用ナプキン、つかいすておむつにおいて、
通気性と防水性を有するポリオレフイン系多孔樹
脂フイルムが防漏材として使用されている。
かかる多孔樹脂フイルムは、高密度ポリエチレ
ン、線状ポリエチレンまたは両者の混合物を樹脂
素材とし、これに炭酸カルシウム、酸化チタン、
焼成クレイ、けいそう土等の無機微細粉末、必要
によりポリエチレンワツクス、液状ブタジエンゴ
ム、液状イソブチレンゴム、液状ポリエチレンワ
ツクス、液状水添ヒマシ油、等の柔軟性改良剤を
配合した組成物を抽出機を用いてフイルム状に溶
融成形後、マンドレル、ロール群の周速差を利用
した延伸装置、またはテンターを用いて延伸成形
することにより製造されている(特開昭57−
47334号、同57−203520号、同58−15538号、同58
−149925号、同58−149303号、同59−62117号、
同59−140235号、同60−6442号)。
また、この多孔樹脂フイルムは電解隔膜として
利用できることも提案されている。
〔従来技術の問題点〕
この多孔樹脂フイルムは無機微細粉末を核とし
て微細な連続空孔を多数有し、表面には大気に連
通した空隙を有する通気性に富む単層の1軸延伸
フイルムまたは2軸延伸フイルムで、つかいすて
おむつの防水カバーシートとして有用である。
この多孔樹脂フイルムをつかいすておむつの防
水カバーシートとして用いるとき、表面に離型紙
を備えた両面粘着テープが止め具として用いられ
赤ちやんの股につかいすておむつを装着した後、
両面粘着テープの表面の離型紙を引き剥し、露呈
した粘着剤で貼着してつかいすておむつを固定す
る。
この粘着テープを多孔樹脂フイルムの誤つた位
置に貼合した場合または貼合した位置を少しずら
せたいとき、粘着テープを貼着しなおすためにつ
かいすておむつより剥離すると、従来の多孔樹脂
2軸延伸フイルムは表面に無機微細粉末が突出、
遊離もしくは樹脂フイルム基材に付着して露出し
ており、前記空孔が円形ないし楕円状であり無機
微細粉末が脱落しやすくなつているので、この無
機微細粉末が粘着テープの粘着面に移動し、粘着
テープの粘着力を低下させる原因となつたり、多
孔樹脂フイルムの表面強度が低いためにフイルム
表面が紙ムケ状に剥離したりする問題がある。
一方、一軸延伸フイルムは、空孔が長尺状であ
り、延伸面積倍率も2軸延伸フイルムのそれより
小さいので無機微細粉末の脱落も2軸延伸フイル
ムより少なく、かつ、表面強度も2軸延伸フイル
ムのそれより強い利点があるが、方向性があると
ともに抗クリープ性に乏しく、おむつカバーが使
用時に伸びきつてゆるんでしまい、防漏性を満足
させることができない。特に引張り破断伸びが
500%を超えるものは好ましくない。
更に、この多孔樹脂フイルムを電解隔膜として
用いた場合、電解液の種類によつては多孔樹脂フ
イルムより突出している無機微細粉末により電解
液が変性したり、無機微細粉末が溶出して電解液
の機能が低下する。
また、種々の穿孔フイルム及びその製造法が提
案されているが、これらのフイルムのうちのある
ものは大気圧においての防水性は発揮するものの
オムツカバーや紙オムツの防漏フイルムに使用さ
れた場合、体重がかかつた部分では漏れが発生す
る。
〔問題点を解決する具体的手段〕
本発明においては、穿孔した熱収縮性樹脂フイ
ルムを熱収縮させることにより通気性を有し、水
防漏性を有する有孔樹脂を用いる。
すなわち、本発明は、熱収縮性樹脂フイルム
に、直径が50〜600ミクロンの孔を10〜250個/cm2
の割合で穿孔を施こし、この熱収縮性樹脂フイル
ムを加熱処理して面積量で10〜70%収縮させて20
℃における透気度が30〜10000秒であり、20℃に
おける透湿度が50〜10000g/m2・24時間・1気
圧である樹脂フイルムを得ることを特徴とする有
孔樹脂フイルムの製造方法を提供するものであ
る。
(熱収縮性樹脂フイルム)
熱収縮性樹脂フイルムは、熱可塑性樹脂フイル
ムを、該樹脂の融点よりも低い温度で、フイルム
の一軸方向または二軸方向に面積して1.3〜70倍、
好ましくは1.3〜50倍延伸することにより得られ
る。
熱可塑性樹脂としては、線状ポリエチレン
(MP約121℃、延伸温度115〜119℃)、高密度ポ
リエチレン(MP約133℃、延伸温度129〜131
℃)、ホモポリプロピレン(MP約164℃、延伸温
度150〜162℃)、プロピレン・エチレンランダム
共重合体(MP約134℃、延伸温度125〜132℃)、
ポリエチレンテレフタレート(MP約247℃、延
伸温度102〜120℃)、ポリスチレンもしくはポリ
塩化ビニル(軟化点約163〜168℃、延伸温度145
〜158℃)、ポリアミド(融点約248℃、延伸温度
120〜180℃)等が挙げられる。なお、括弧内の融
点(MP)と延伸温度は例示であつて、融点の異
なる同種の樹脂についても、樹脂の融点(ポリス
チレン、ポリ塩化ビニルのような非晶性樹脂のと
きは軟化点)を基準にして略同幅程度の温度差を
目安に延伸温度を選択する。
延伸は、マンドレル、テンター、ロール群の周
速差を利用して行なう。延伸倍率は一軸延伸フイ
ルムで1.3〜10倍、二軸延伸フイルムで1.6〜70倍
である。
フイルムの成形はインフレーシヨン法、T−ダ
イ法が一般的である。穿孔される前の熱収縮性樹
脂フイルムの肉厚は10〜100ミクロンが通常、市
場より容易に入手できる。例えば線状ポリエチレ
ン製の熱収縮性樹脂フイルムは、(株)興人よりコー
ジンポリセツト−Uの商品名で、ポリ塩化ビニル
製の熱収縮性樹脂フイルムは三菱樹脂(株)よりヒミ
レツクス−MBSの商品名で、ポリプロピレン製
の熱収縮性樹脂フイルムは、(株)興人よりコージン
ポリセツトの商品で販売されている。
(穿孔)
熱収縮性樹脂フイルムには、孔が10〜250個/
cm2の割合で穿孔される。穿孔手段としては針、レ
ザー光線が利用できる。勿論、熱針も使用でき
る。孔の直径は、50〜600ミクロンが好ましい。
現在の穿孔手段では50ミクロン未満の孔を穿つこ
とが機械的に困難である。600ミクロンを越える
孔では、収縮により樹脂フイルムに水防漏性を付
与することが困難である。
(熱収縮)
熱収縮は、穿孔した熱収縮性樹脂フイルムを加
熱炉内で熱収縮させる。熱収縮させる温度は、熱
収縮性フイルム製造時の延伸温度、熱セツト温度
を参考に、これら温度より若干高めの温度(1〜
3℃高い温度)と樹脂フイルムの温度がなつたと
きに熱収縮性樹脂フイルムの収縮が起る。従つ
て、加熱炉内の温度およびフイルムの加熱炉内の
滞在時間はかかる熱量を樹脂フイルムが吸収する
よう成形サイクル、品質面、経済面から決定すべ
きである。
例えば、加熱炉が一台で炉内の温度が均一のと
きは、延伸温度ないし熱セツト温度よりも2〜10
℃高い温度に炉内温度を設定する。加熱炉内の温
度を3段階に替え、例えば延伸温度が119℃の線
状ポリエチレン熱収縮フイルムのとき、最初の温
度を135℃、次の温度を115℃、最後の温度を122
℃として熱処理温度を短縮させることができる。
また、3台の熱風炉を用い、上記温度に設定し、
熱収縮性フイルムをこれら熱風炉に導き熱処理し
てもよい。
この熱収縮処理によりフイルムは面積で10〜70
%収縮する。この収縮により穿孔された孔が収縮
する一方、穿孔カスは充分な収縮が起らないた
め、熱処理されたフイルムに水防漏性が付与され
るものと推定される。
熱収縮率(熱処理された後のフイルムの表面
積/熱処理される前のフイルムの表面積の百分
率)は、熱収縮性樹脂フイルムを製造する際の延
伸倍率に左右されるが、この延伸倍率と略同一と
した方が有孔フイルムに収縮むらがなく、外観の
優れたものとなるので好ましい。
(有孔樹脂フイルム)
熱処理により得られた有孔樹脂フイルムは、
JIS Z−0208に準処して20℃で測定した透湿度が
50〜10000g/m2・24時間・1気圧、好ましくは
1000〜6000g/m2・24時間・1気圧であり、次の
方法で測定した20℃における透気度が30〜10000
秒、好ましくは100〜3000秒である。
透気度の測定法
JIS P−8117に準処して作られた王研式透気
度・平滑度試験機(旭精工製)を用いて測定透気
度、透湿度が前範囲を外れると、この有孔樹脂フ
イルムをおむつの防水カバーや使いすて生理用ナ
プキンの防漏材として用いたとき、むれがおきや
すいか、防液性がない。
実施例 1
肉厚20ミクロン、縦200mm、横200mmの(株)興人製
線状ポリエチレン製の透明な熱収縮性フイルム
“コージンポリセツトU”(商品名)に注射針を用
いて直径200ミクロンの孔を1cm2あたり25個の割
合で穿孔した。
この穿孔フイルムを炉内温度120℃の熱風乾燥
炉内に導き、同炉内で1分間放置して熱収縮(約
40%収縮)させ、ついで炉外に導き有孔樹脂フイ
ルムを得た。
この有孔樹脂フイルムの透湿度は、1700g/
m2・24時間・1気圧で、透気度は2300秒であつ
た。また、次の方法で水防漏性を検査したとこ
ろ、漏水は無かつた。
水防漏性試験:
直径80mmφの瀘紙の上に縦100mm、横100mmの本
発明の有孔樹脂フイルムをかぶせ、有孔樹脂フイ
ルムの中央部に蒸溜水を0.3c.c.滴下した。この有
孔樹脂フイルムの上に、横120mm、縦120mm、重量
200gのアクリル樹脂板を有孔樹脂フイルムを覆
う様に載せた。
この時、水滴が瀘紙に吸い込まれることなく有
孔樹脂フイルムの周辺方向に拡がれば有孔樹脂フ
イルムの水防漏性は良好であり、孔を通して下側
の瀘紙に吸水されれば有孔樹脂フイルムの水防漏
性は不良である。
実施例 2〜3
熱風炉内の収縮性樹脂フイルムの保持時間を変
えて収縮量を40%の代りに20%または60%とする
他は実施例1と同様にして有孔樹脂フイルムを得
た。
実施例 4〜5
穿孔径200μを、80μまたは500μに変更する他は
実施例1と同様にして有孔樹脂フイルムを得た。
比較例 1
実施例1に用いた熱収縮性樹脂フイルム“コー
ジンポリセツトU”を40%収縮させて無孔フイル
ムを得た。
比較例 2〜4
実施例1において、収縮量を0%、5%または
80%に変える他は実施例1と同様にして有孔フイ
ルムを得た。
これら樹脂フイルムの物性を表1に示す。
【表】[Detailed Description of the Invention] [Industrial Application Field] The porous resin film obtained by carrying out the present invention can be used as a leak-proof material for disposable diapers, sanitary napkins, etc., as an external material for electrolytic diaphragms, and structures. It is useful as a moisture-proof membrane interposed between interior materials. [Prior art] In sanitary napkins and disposable diapers,
Polyolefin porous resin film, which has breathability and waterproof properties, is used as a leak-proof material. Such porous resin film uses high-density polyethylene, linear polyethylene, or a mixture of both as a resin material, and contains calcium carbonate, titanium oxide,
Extract a composition containing inorganic fine powder such as fired clay or diatomaceous earth, and if necessary, a flexibility improver such as polyethylene wax, liquid butadiene rubber, liquid isobutylene rubber, liquid polyethylene wax, liquid hydrogenated castor oil, etc. It is manufactured by melt-forming into a film using a machine, and then stretching and forming using a mandrel, a stretching device that utilizes the peripheral speed difference between a group of rolls, or a tenter.
No. 47334, No. 57-203520, No. 58-15538, No. 58
−149925, No. 58-149303, No. 59-62117,
59-140235, 60-6442). It has also been proposed that this porous resin film can be used as an electrolytic diaphragm. [Problems with the prior art] This porous resin film has a large number of fine continuous pores with a core of inorganic fine powder, and a highly air permeable single layer uniaxially stretched film with voids communicating with the atmosphere on the surface. This biaxially stretched film is useful as a waterproof cover sheet for disposable diapers. When this porous resin film is used as a waterproof cover sheet for disposable diapers, a double-sided adhesive tape with release paper on the surface is used as a fastener, and after the diaper is attached to the baby's crotch,
Peel off the release paper on the surface of the double-sided adhesive tape and use the exposed adhesive to fix the disposable diaper. When this adhesive tape is attached to the wrong position of the porous resin film or when you want to slightly shift the attached position, you can use it to reapply the adhesive tape and peel it off from the diaper. The stretched film has fine inorganic powder protruding from the surface.
The pores are either free or attached to the resin film base material and exposed, and the pores are circular or elliptical, making it easy for the inorganic fine powder to fall off, so this inorganic fine powder moves to the adhesive surface of the adhesive tape. However, since the surface strength of the porous resin film is low, the surface of the film may peel off like paper flakes. On the other hand, in a uniaxially stretched film, the pores are long and the stretching area ratio is smaller than that of a biaxially stretched film, so the amount of inorganic fine powder falling off is less than that of a biaxially stretched film, and the surface strength is also lower than that of a biaxially stretched film. Although it has stronger advantages than film, it has directionality and poor creep resistance, and the diaper cover stretches and loosens during use, making it impossible to satisfy leak-proof properties. Especially the tensile elongation at break
Anything over 500% is not desirable. Furthermore, when this porous resin film is used as an electrolytic diaphragm, depending on the type of electrolyte, the electrolyte may be denatured by the inorganic fine powder that protrudes from the porous resin film, or the inorganic fine powder may be eluted and the electrolyte may deteriorate. Function deteriorates. In addition, various perforated films and their manufacturing methods have been proposed, but although some of these films exhibit waterproofness at atmospheric pressure, they do not work well when used as leak-proof films for diaper covers or disposable diapers. , leakage occurs in areas where weight is applied. [Specific Means for Solving the Problems] In the present invention, a perforated resin having air permeability and water leakage resistance is used by heat-shrinking a perforated heat-shrinkable resin film. That is, the present invention provides a heat-shrinkable resin film with 10 to 250 holes/cm 2 with a diameter of 50 to 600 microns.
This heat-shrinkable resin film is then heat-treated to shrink by 10 to 70% in terms of area.
A method for producing a perforated resin film characterized by obtaining a resin film having an air permeability of 30 to 10,000 seconds at 20°C and a moisture permeability of 50 to 10,000 g/ m2 /24 hours/1 atm at 20°C. This is what we provide. (Heat-shrinkable resin film) Heat-shrinkable resin film is made by heating a thermoplastic resin film at a temperature lower than the melting point of the resin, and increasing the area by 1.3 to 70 times the area in one or two axis directions of the film.
It is preferably obtained by stretching 1.3 to 50 times. Thermoplastic resins include linear polyethylene (MP approx. 121℃, stretching temperature 115-119℃), high-density polyethylene (MP approx. 133℃, stretching temperature 129-131℃),
℃), homopolypropylene (MP approx. 164℃, stretching temperature 150-162℃), propylene-ethylene random copolymer (MP approx. 134℃, stretching temperature 125-132℃),
Polyethylene terephthalate (MP approx. 247℃, stretching temperature 102-120℃), polystyrene or polyvinyl chloride (softening point approx. 163-168℃, stretching temperature 145℃)
~158℃), polyamide (melting point approx. 248℃, stretching temperature
120 to 180°C), etc. Note that the melting point (MP) and stretching temperature in parentheses are examples, and the melting point (softening point in the case of amorphous resins such as polystyrene and polyvinyl chloride) of the same resin with different melting points is also The stretching temperature is selected based on a temperature difference of approximately the same width as a reference. Stretching is carried out using the difference in circumferential speed between the mandrel, tenter, and roll group. The stretching ratio is 1.3 to 10 times for a uniaxially stretched film, and 1.6 to 70 times for a biaxially stretched film. Films are generally formed by an inflation method or a T-die method. The thickness of the heat-shrinkable resin film before perforation is usually 10 to 100 microns and is easily available on the market. For example, a heat-shrinkable resin film made of linear polyethylene is manufactured by Kojin Co., Ltd. under the trade name Kojin Polyset-U, and a heat-shrinkable resin film made of polyvinyl chloride is manufactured by Mitsubishi Plastics Co., Ltd. under the trade name Himilex-MBS. A heat-shrinkable resin film made of polypropylene is sold by Kojin Co., Ltd. under the trade name Kojin Polyset. (Perforation) Heat-shrinkable resin film has 10 to 250 holes/
Perforated at the rate of cm 2 . A needle or a laser beam can be used as the perforation means. Of course, you can also use a hot needle. The diameter of the pores is preferably between 50 and 600 microns.
It is mechanically difficult to drill holes smaller than 50 microns with current drilling means. With pores larger than 600 microns, it is difficult to provide water leakage properties to the resin film due to shrinkage. (Heat Shrinkage) Heat shrinkage involves heat shrinking a perforated heat-shrinkable resin film in a heating furnace. The temperature for heat shrinking is a temperature slightly higher than these temperatures (1 to
Shrinkage of the heat-shrinkable resin film occurs when the temperature of the resin film becomes lower than the temperature (3°C higher). Therefore, the temperature in the heating furnace and the residence time of the film in the heating furnace should be determined from the viewpoints of molding cycle, quality, and economy so that the resin film can absorb this amount of heat. For example, when there is one heating furnace and the temperature inside the furnace is uniform, it is 2 to 10 degrees lower than the drawing temperature or heat set temperature.
Set the furnace temperature to ℃ higher. Change the temperature in the heating furnace in three stages. For example, when drawing a linear polyethylene heat shrink film with a stretching temperature of 119°C, the first temperature is 135°C, the next temperature is 115°C, and the final temperature is 122°C.
℃, the heat treatment temperature can be shortened.
In addition, using three hot air stoves, the temperature was set to the above,
The heat-shrinkable film may be introduced into these hot air ovens for heat treatment. This heat shrinking process results in a film with an area of 10 to 70
% shrinkage. While the perforated holes shrink due to this shrinkage, the perforated dregs do not shrink sufficiently, and it is therefore presumed that the heat-treated film is imparted with water leakproof properties. The heat shrinkage rate (surface area of the film after heat treatment/percentage of the surface area of the film before heat treatment) depends on the stretching ratio when manufacturing the heat-shrinkable resin film, but it is approximately the same as this stretching ratio. This is preferable because the perforated film has no uneven shrinkage and has an excellent appearance. (Porous resin film) The porous resin film obtained by heat treatment is
Moisture permeability measured at 20℃ in accordance with JIS Z-0208
50-10000g/m 2 , 24 hours, 1 atm, preferably
1000-6000g/ m2 , 24 hours, 1 atm, and the air permeability at 20℃ measured by the following method is 30-10000
seconds, preferably 100 to 3000 seconds. Measuring method of air permeability: If the measured air permeability and moisture permeability are out of the range, When this perforated resin film is used as a waterproof cover for diapers or as a leak-proof material for disposable sanitary napkins, it tends to get stuffy or lacks liquid-proof properties. Example 1 A transparent heat-shrinkable film made of linear polyethylene "Kojin Polyset U" (trade name) manufactured by Kojin Co., Ltd. with a wall thickness of 20 microns, a length of 200 mm, and a width of 200 mm was made to have a diameter of 200 microns using a syringe needle. holes were drilled at a rate of 25 holes per cm 2 . This perforated film was introduced into a hot air drying oven with an internal temperature of 120°C, and left in the oven for 1 minute to cause heat shrinkage (approx.
40% shrinkage) and then led out of the furnace to obtain a perforated resin film. The moisture permeability of this perforated resin film is 1700g/
m 2 / 24 hours / 1 atm, the air permeability was 2300 seconds. In addition, when the water leak resistance was tested using the following method, there was no water leak. Water leak resistance test: A perforated resin film of the present invention measuring 100 mm in length and 100 mm in width was placed on a filter paper with a diameter of 80 mm, and 0.3 cc of distilled water was dropped into the center of the perforated resin film. On this perforated resin film, the width 120mm, height 120mm, weight
A 200 g acrylic resin plate was placed so as to cover the perforated resin film. At this time, if the water droplets spread toward the periphery of the perforated resin film without being sucked into the filter paper, the water leakage properties of the perforated resin film are good, and if the water is absorbed by the lower filter paper through the holes, then there is The water leakage properties of the porous resin film are poor. Examples 2 to 3 A perforated resin film was obtained in the same manner as in Example 1, except that the holding time of the shrinkable resin film in the hot air stove was changed and the amount of shrinkage was changed to 20% or 60% instead of 40%. . Examples 4-5 A perforated resin film was obtained in the same manner as in Example 1, except that the perforation diameter was changed from 200μ to 80μ or 500μ. Comparative Example 1 The heat-shrinkable resin film "Kojin Polyset U" used in Example 1 was shrunk by 40% to obtain a non-porous film. Comparative Examples 2 to 4 In Example 1, the amount of shrinkage was 0%, 5% or
A perforated film was obtained in the same manner as in Example 1 except that the ratio was changed to 80%. Table 1 shows the physical properties of these resin films. 【table】
Claims (1)
クロンの孔を10〜250個/cm2の割合で穿孔を施こ
し、この熱収縮性樹脂フイルムを加熱処理して面
積量で10〜70%収縮させて20℃における透気度が
30〜10000秒であり、20℃における透湿度が50〜
10000g/m2・24時間・1気圧である樹脂フイル
ムを得ることを特徴とする有孔樹脂フイルムの製
造方法。1. A heat-shrinkable resin film is perforated with holes of 50-600 microns in diameter at a rate of 10-250 holes/ cm2 , and the heat-shrinkable resin film is heat-treated to 10-70% in area. Air permeability at 20℃ after shrinking
30~10000 seconds, moisture permeability at 20℃ is 50~
A method for producing a perforated resin film, characterized by obtaining a resin film having a pressure of 10,000 g/m 2 for 24 hours and 1 atm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60290177A JPS62148246A (en) | 1985-12-23 | 1985-12-23 | Manufacture of perforated resin film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60290177A JPS62148246A (en) | 1985-12-23 | 1985-12-23 | Manufacture of perforated resin film |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62148246A JPS62148246A (en) | 1987-07-02 |
| JPH0564096B2 true JPH0564096B2 (en) | 1993-09-13 |
Family
ID=17752743
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60290177A Granted JPS62148246A (en) | 1985-12-23 | 1985-12-23 | Manufacture of perforated resin film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62148246A (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6323936A (en) * | 1986-07-17 | 1988-02-01 | Dainippon Printing Co Ltd | Production of perforated film |
| GB9015448D0 (en) * | 1990-07-13 | 1990-08-29 | Lanmark Consultants Ltd | Improvements in or relating to flow control |
| NL9102189A (en) * | 1991-12-30 | 1993-07-16 | Dsm Nv | PROCESS FOR MANUFACTURING A HIGH CRACK STRENGTH POROUS FOIL |
| JPH07119004B2 (en) * | 1992-12-03 | 1995-12-20 | 下村化工紙株式会社 | Method of perforating through holes in synthetic resin film in composite film of Japanese paper and synthetic resin |
| US20170239093A1 (en) * | 2014-11-12 | 2017-08-24 | Asahi Kasei Kabushiki Kaisha | Perforated Plastic Film |
| WO2018116447A1 (en) * | 2016-12-22 | 2018-06-28 | 平岡織染株式会社 | Antifouling sheet, antifouling sheet joined body, and method for manufacturing antifouling sheet joined body |
-
1985
- 1985-12-23 JP JP60290177A patent/JPS62148246A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62148246A (en) | 1987-07-02 |
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