JPH0331737B2 - - Google Patents

Info

Publication number
JPH0331737B2
JPH0331737B2 JP7317785A JP7317785A JPH0331737B2 JP H0331737 B2 JPH0331737 B2 JP H0331737B2 JP 7317785 A JP7317785 A JP 7317785A JP 7317785 A JP7317785 A JP 7317785A JP H0331737 B2 JPH0331737 B2 JP H0331737B2
Authority
JP
Japan
Prior art keywords
film
holes
discharge treatment
synthetic resin
filler
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
JP7317785A
Other languages
Japanese (ja)
Other versions
JPS61230922A (en
Inventor
Katsuhito Nagao
Susumu Miki
Keijiro Hamano
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.)
Okura Industrial Co Ltd
Original Assignee
Okura Industrial Co 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 Okura Industrial Co Ltd filed Critical Okura Industrial Co Ltd
Priority to JP7317785A priority Critical patent/JPS61230922A/en
Publication of JPS61230922A publication Critical patent/JPS61230922A/en
Publication of JPH0331737B2 publication Critical patent/JPH0331737B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Treatments Of Macromolecular Shaped Articles (AREA)
  • 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)

Description

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

〔産業上の利用分野〕 本発明は透湿性に優れ、更に適当な通水性をも
有する合成樹脂脂有孔フイルムの連続製造方法に
関するものである。 〔従来の技術〕 従来、合成樹脂有孔フイルムの製造方法とし
て、充填剤を添加したフイルムを延伸する方法
(特開昭57−203520)、充填剤を添加したフイルム
を溶剤に浸漬し充填剤を溶出する方法(特公昭58
−30899)、予め針等で貫通孔を穿設したフイルム
に放電処理を施す方法(特開昭54−58775)等が
知られている。 〔発明が解決しようとする問題点〕 充填剤を添加し延伸した合成樹脂フイルムはそ
の厚み方向に於て複数の層状に破断孔が発生し、
それらが連なつてフイルムの一面から他面へ通じ
ているので該合成樹脂フイルムは透湿性は有する
が十分でなく、通水性はほとんど有しないもので
あつた。又、延伸倍率を上げることにより透湿性
の向上を計ると、破断孔の大きさが不均一にな
り、安定した有孔フイルムの製造が行えなかつ
た。 充填剤をを添加したフイルムを溶剤に浸漬する
方法は連続製造が困難であつた。 又、予め針等で貫通孔を穿設したフイルムに放
電処理を施す方法は貫通孔の孔径が数m/m以上
という大きいものしか得られなかつた。 〔問題点を解決するための手段〕 本発明は無機質及び/又は有機質の充填剤を添
加した合成樹脂フイルム(以下フイルムという)
を少くとも一方向に1.05倍以上延伸して、該フイ
ルムに破断孔を生ぜしめしかる後放電処理を施す
ことにより孔径数10μ〜数100μの均一な貫通孔を
連続的に穿設するものである。 以下、本発明の一実施例を示す図面に基いて説
明する。 第1図は本発明の有孔フイルムの連続製造に係
る装置の概略図であり、第2図は延伸後のフイル
ムに放電処理を施す放電処理装置の斜視図であ
る。 第1図に於て、押出機1の先端に設けられてい
る成形ダイ2より押出されたフイルム3を必要に
応じて予熱ロール4,5で適宜温度に予熱し、ピ
ンチロール6,7で縦方向に1.0倍以上延伸して
前記フイルム3に微細な破断孔を生じさせる。し
かる後高電圧発生装置10より送電される高電圧
の印加された一対の電極8,9間に前記フイルム
3を導き放電処理を施し均一な大きさの貫通孔を
穿設する。 本発明に於て用いられる合成樹としてはポリエ
チレン、ポリプロピレン、ポリ塩化ビニル、ポリ
スチレン、ポリエステル等である。フイルムに添
加する充填剤としては炭酸カルシウム、タルクク
レー、シリカ、珪藻土、硫酸バリウム、酸化チタ
ン等の無機質のもの、もみがら粉、デンプン、木
粉、パルプ粉等の有機質のもの、或いは前記無機
質と有機質の充填剤を混和したものが用いられ
る。充填剤の添加量は合成樹脂の20〜200重量%
好ましく20%未満ではフイルムに生じる破断孔の
数が少なく良好な有孔フイルムが得られない。
又、200重量%を越える場合はフイルムの強度が
低下し好ましくない。充填剤の大きさは0.5〜
200μが好ましい。 フイルムの延伸は1方向、2方向のいずれでも
よいが一方向の延伸が操作が簡単であるので好ま
しい。延伸倍率は充填剤の大き、添加率、延伸温
度により適宜決定されるが、1.05〜10倍の範囲が
好ましく、1.05倍未満では破断孔が発生しなく、
10倍を越すと破断孔が不均一になり、一部が異常
に大きくなつたり、又フイルムの切断が生じ作業
性が低下するので好ましくない。 延伸に際してフイルムを適宜温度に予熱すると
破断孔の発生を抑制したり或いは延伸ムラを少な
くすることができる。 又、電極8の端子11の密度によりフイルムの
貫通孔の密度を調節することができる。更に充填
剤の添加されたフイルムを延伸する際、予熱ロー
ル4,5の一部分のみを加熱することにより、フ
イルムが部分的に加熱される。このフイルムの加
熱された部分は他の部分に比し破断孔の発生が少
なくなり、同一フイルム内での破断孔の密度を変
えることができる。 〔実施例〕 実施例 1 平均粒径2μの炭酸カルシウムを50重量%添加
した厚み0.06m/mの高圧法ポリエチレンフイル
ムを80℃に予熱後1方向2倍延伸し14KVの電圧
で放電処理を施し厚み0.03m/mの有効フイルム
を得た。 実施例 2 平均粒径5μのタルクを50重量%添加した厚み
0.1m/mの塩化ビニルフイルムを80℃に予熱後1
方向に4倍延伸し14KVの電圧で放電処理を施し
厚み0.03m/mの有孔フイルムを得た。 実施例 3 平均粒径100μのもみがら粉を25重量%添加し
た厚み0.3m/mのポリプロピレンフイルムを135
℃に予熱後1方向に3倍延伸し14KVの電圧で放
電処理を施し厚み0.15m/mの有孔フイルムを得
た。 比較例 1〜3 実施例1〜3の有孔フイルムを製造方法に於て
放電処理を施さないものをそれぞれの実施例に対
応する比較例とする。 各実施例及び比較例の製造条件、得られたフイ
ルムの透湿度、通水性等を第1表にまとめる。
[Industrial Field of Application] The present invention relates to a method for continuously producing a perforated synthetic resin film having excellent moisture permeability and appropriate water permeability. [Prior Art] Conventionally, methods for producing perforated synthetic resin films include stretching a film to which a filler has been added (Japanese Patent Application Laid-open No. 57-203520), and immersing a film to which a filler has been added in a solvent to remove the filler. Method of elution (Special Publication 1978
-30899), and a method in which a film in which through holes are previously formed with a needle or the like is subjected to electrical discharge treatment (Japanese Patent Application Laid-Open No. 54-58775). [Problems to be solved by the invention] A synthetic resin film that has been stretched with a filler added has fracture holes in multiple layers in the thickness direction.
Since they are continuous and communicate from one side of the film to the other, the synthetic resin film has moisture permeability, but it is not sufficient and has almost no water permeability. Furthermore, when the moisture permeability was improved by increasing the stretching ratio, the sizes of the fractured holes became non-uniform, making it impossible to stably produce a perforated film. Continuous production is difficult in the method of immersing a filler-added film in a solvent. In addition, the method of applying electrical discharge treatment to a film in which through-holes have been previously formed with a needle or the like can only produce large through-holes with diameters of several m/m or more. [Means for solving the problems] The present invention provides a synthetic resin film (hereinafter referred to as a film) to which an inorganic and/or organic filler is added.
By stretching the film by at least 1.05 times in one direction and subjecting the film to a post-discharge treatment that produces break holes, uniform through-holes with a diameter of several tens of microns to several hundred microns are continuously formed. . DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic view of an apparatus for continuous production of a perforated film according to the present invention, and FIG. 2 is a perspective view of an electric discharge treatment apparatus for subjecting the stretched film to electric discharge treatment. In FIG. 1, a film 3 extruded from a forming die 2 provided at the tip of an extruder 1 is preheated to an appropriate temperature with preheating rolls 4 and 5 as necessary, and then vertically with pinch rolls 6 and 7. The film 3 is stretched by a factor of 1.0 or more in the direction of the film 3 to form minute holes. Thereafter, the film 3 is guided between a pair of electrodes 8 and 9 to which a high voltage is applied, which is transmitted from the high voltage generator 10, and subjected to a discharge treatment to form through holes of uniform size. The synthetic resins used in the present invention include polyethylene, polypropylene, polyvinyl chloride, polystyrene, polyester, and the like. Fillers added to the film include inorganic fillers such as calcium carbonate, talcum clay, silica, diatomaceous earth, barium sulfate, and titanium oxide, organic fillers such as rice husk powder, starch, wood flour, and pulp powder, or the above-mentioned inorganic and organic fillers. A mixture of fillers is used. The amount of filler added is 20 to 200% by weight of the synthetic resin.
Preferably, if it is less than 20%, the number of breakage holes generated in the film is small and a good perforated film cannot be obtained.
Moreover, if it exceeds 200% by weight, the strength of the film decreases, which is not preferable. The size of the filler is 0.5~
200μ is preferred. The film may be stretched in either one direction or two directions, but unidirectional stretching is preferred because it is easier to operate. The stretching ratio is appropriately determined depending on the size of the filler, the addition rate, and the stretching temperature, but it is preferably in the range of 1.05 to 10 times, and if it is less than 1.05 times, break holes will not occur.
If it exceeds 10 times, the fracture holes will become non-uniform, some will become abnormally large, and the film will be cut, which will reduce workability, which is not preferable. If the film is preheated to an appropriate temperature during stretching, the occurrence of break holes can be suppressed or uneven stretching can be reduced. Furthermore, the density of the through holes in the film can be adjusted by adjusting the density of the terminals 11 of the electrodes 8. Furthermore, when stretching the film to which the filler has been added, the film is partially heated by heating only a portion of the preheating rolls 4 and 5. The heated portion of the film has fewer fracture holes than other portions, and the density of fracture holes within the same film can be varied. [Example] Example 1 A high-pressure polyethylene film with a thickness of 0.06 m/m to which 50% by weight of calcium carbonate with an average particle size of 2 μ was added was preheated to 80°C, stretched twice in one direction, and subjected to electric discharge treatment at a voltage of 14 KV. An effective film with a thickness of 0.03m/m was obtained. Example 2 Thickness with addition of 50% by weight of talc with an average particle size of 5μ
1 after preheating 0.1m/m vinyl chloride film to 80℃
The film was stretched 4 times in the direction and subjected to discharge treatment at a voltage of 14 KV to obtain a perforated film with a thickness of 0.03 m/m. Example 3 A polypropylene film with a thickness of 0.3 m/m to which 25% by weight of rice husk powder with an average particle size of 100 μm was added was made into 135
After preheating to ℃, it was stretched 3 times in one direction and subjected to discharge treatment at a voltage of 14 KV to obtain a perforated film with a thickness of 0.15 m/m. Comparative Examples 1 to 3 The perforated films of Examples 1 to 3 were not subjected to discharge treatment in the manufacturing method as comparative examples corresponding to the respective examples. Table 1 summarizes the manufacturing conditions, moisture permeability, water permeability, etc. of the obtained films for each Example and Comparative Example.

〔発明の効果〕〔Effect of the invention〕

本発明の有孔フイルムの製造方法は、充填剤を
添加したフイルムを延伸して破断孔を生ぜしめ、
しかる後放電処理を施して貫通孔を穿設するの
で、均一で微小な貫通孔を連続的に穿設すること
ができるものである。 更に延伸による破断孔と放電処理による貫通孔
の相乗効果により透湿性に優れ、更に適当な通水
性をも有するフイルムが得られるものである。
The method for producing a perforated film of the present invention includes stretching a film to which a filler has been added to create break holes;
Since the through-holes are formed by performing a discharge treatment after that, it is possible to continuously form uniform and minute through-holes. Further, due to the synergistic effect of the fracture holes caused by stretching and the through holes caused by discharge treatment, a film can be obtained which has excellent moisture permeability and also has appropriate water permeability.

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

第1図は本発明の有孔フイルムの連続製造に係
る装置の概略図であり、第2図は延伸後のフイル
ムに放電処理を施す装置の斜視図である。 3…合成樹脂フイルム、4,5…予熱ロール、
6,7…ピンチロール、8,9…電極、11…端
子。
FIG. 1 is a schematic diagram of an apparatus for continuous production of a perforated film according to the present invention, and FIG. 2 is a perspective view of an apparatus for subjecting the stretched film to electrical discharge treatment. 3...Synthetic resin film, 4,5...Preheating roll,
6, 7...pinch roll, 8, 9...electrode, 11...terminal.

Claims (1)

【特許請求の範囲】[Claims] 1 無機質及び/又は有機質の充填剤を合成樹脂
の20〜200重量%添加した合成樹脂フイルムを少
くとも一方向に1.05倍以上延伸し、該フイルムを
高電圧の印加された一対の電極間に導き放電処理
を施すことにより貫通孔を穿設することを特徴と
する合成樹脂有孔フイルムの連続製造方法。
1. A synthetic resin film containing 20 to 200% by weight of the synthetic resin of an inorganic and/or organic filler is stretched at least 1.05 times in one direction, and the film is guided between a pair of electrodes to which a high voltage is applied. 1. A continuous manufacturing method for a perforated synthetic resin film, characterized in that through-holes are formed by subjecting it to electrical discharge treatment.
JP7317785A 1985-04-05 1985-04-05 Continuous manufacture of synthetic resin porous film Granted JPS61230922A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7317785A JPS61230922A (en) 1985-04-05 1985-04-05 Continuous manufacture of synthetic resin porous film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7317785A JPS61230922A (en) 1985-04-05 1985-04-05 Continuous manufacture of synthetic resin porous film

Publications (2)

Publication Number Publication Date
JPS61230922A JPS61230922A (en) 1986-10-15
JPH0331737B2 true JPH0331737B2 (en) 1991-05-08

Family

ID=13510595

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7317785A Granted JPS61230922A (en) 1985-04-05 1985-04-05 Continuous manufacture of synthetic resin porous film

Country Status (1)

Country Link
JP (1) JPS61230922A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03100028A (en) * 1989-09-13 1991-04-25 Tokuyama Soda Co Ltd Porous film

Also Published As

Publication number Publication date
JPS61230922A (en) 1986-10-15

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