JP2618463B2 - Stretched film manufacturing method - Google Patents

Stretched film manufacturing method

Info

Publication number
JP2618463B2
JP2618463B2 JP1196589A JP1196589A JP2618463B2 JP 2618463 B2 JP2618463 B2 JP 2618463B2 JP 1196589 A JP1196589 A JP 1196589A JP 1196589 A JP1196589 A JP 1196589A JP 2618463 B2 JP2618463 B2 JP 2618463B2
Authority
JP
Japan
Prior art keywords
stretching
film
stretched
stretched film
flow direction
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
Application number
JP1196589A
Other languages
Japanese (ja)
Other versions
JPH02194035A (en
Inventor
康弘 藤井
従一 辻
松村  秀司
一 六鹿
Original Assignee
三井東圧化学株式会社
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 三井東圧化学株式会社 filed Critical 三井東圧化学株式会社
Priority to JP1196589A priority Critical patent/JP2618463B2/en
Publication of JPH02194035A publication Critical patent/JPH02194035A/en
Application granted granted Critical
Publication of JP2618463B2 publication Critical patent/JP2618463B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、流れ方向(MD)に対して垂直な方向(TD)
に延伸し、更に流れ方向(MD)に延伸された多孔質の延
伸フィルム製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a direction (TD) perpendicular to a flow direction (MD).
And a method for producing a porous stretched film which is further stretched in the machine direction (MD).

〔従来の技術〕[Conventional technology]

多孔質の延伸フィルムを製造する場合に、TD延伸工程
の後にMD延伸工程に行う延伸フィルム製造方法では、MD
延伸時に弱延伸すると延伸むらが発生し、強延伸すると
延伸切れが起こる等のトラブルが発生し易く、安定した
連続延伸を行うことは困難である。
When manufacturing a porous stretched film, in the stretched film manufacturing method performed in the MD stretching step after the TD stretching step, MD
When the film is weakly stretched during stretching, uneven stretching occurs, and when the film is strongly stretched, troubles such as breakage of the film easily occur, and it is difficult to perform stable continuous stretching.

TD延伸後のMD延伸をトラブルの生じない安定状態でMD
への延伸倍率を向上させ、物性バランスの優れた二軸延
伸フィルムを製造するには、これまでの延伸フィルム製
造方法を見直さなければならなかった。
MD stretching after TD stretching in stable state without trouble
In order to improve the draw ratio of the stretched film to produce a biaxially stretched film having an excellent balance of physical properties, the conventional method for producing a stretched film had to be reviewed.

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

本発明の目的は延伸むら及び延伸切れ等のトラブルが
なく、しかもTDとMDの物性バランスが優れ、更にTD延伸
後の高倍率のMD延伸でありながら安定的にMD延伸を行い
得る多孔質の延伸フィルム製造方法を提供することにあ
る。
The object of the present invention is that there is no trouble such as uneven stretching and stretching breakage, and furthermore, the physical properties of TD and MD are excellent, and furthermore, it is possible to carry out MD stretching stably while performing MD stretching at a high magnification after TD stretching. It is to provide a method for producing a stretched film.

〔課題を解決するための手段〕[Means for solving the problem]

本発明者らは、上記目的を達成するため鋭意検討し、
ついに本発明に到った。
The present inventors have diligently studied to achieve the above object,
Finally, the present invention has been reached.

即ち、フィルムを流れ方向に対して垂直な方向に延伸
し、更に流れ方向に延伸する多孔質の延伸フィルム製造
方法において、流れ方向に対して垂直な方向に少なくと
も2倍延伸されたフィルムを流れ方向に対して垂直な方
向に10%から50%収縮させた後、流れ方向に延伸するこ
と特徴とする延伸フィルム製造方法である。
That is, in a method for producing a porous stretched film in which the film is stretched in a direction perpendicular to the flow direction and further stretched in the flow direction, the film stretched at least two times in the direction perpendicular to the flow direction is formed. This is a method for producing a stretched film, wherein the film is contracted by 10% to 50% in a direction perpendicular to the film and then stretched in a flow direction.

本発明の多孔質の延伸フィルム製造方法は未延伸フィ
ルムをTD延伸後、TD延伸機出口からMD延伸機入り口迄の
間で強制的に熱収縮させる。熱収縮はTD延伸温度以上、
樹脂の溶融温度−5℃以下でTDへ10%から50%の範囲で
行う。好ましくは20%〜35%である。
In the method for producing a porous stretched film of the present invention, the unstretched film is forcibly heat-shrinked from the outlet of the TD stretcher to the entrance of the MD stretcher after TD stretching. Heat shrinkage is above TD stretching temperature,
It is performed in the range of 10% to 50% to TD at a resin melting temperature of -5 ° C or less. Preferably it is 20% to 35%.

温度がTD延伸温度未満の場合はフィルムが熱収縮し難
く、樹脂溶融温度−5℃を越えるとフィルムの多孔性が
得られ難くなる。また、熱収縮が10%未満の場合はMD延
伸時にむらが生じたり、延伸切れが発生し、50%を越え
ると物性バランスがとり難くなる。
When the temperature is lower than the TD stretching temperature, the film is unlikely to be thermally shrunk, and when the temperature exceeds the resin melting temperature of −5 ° C., it is difficult to obtain porosity of the film. If the heat shrinkage is less than 10%, unevenness or stretching breakage occurs during MD stretching, and if it exceeds 50%, it becomes difficult to balance physical properties.

上記のような強制的な熱収縮を行った後に、適温で十
分に加熱しMD延伸を行うならば、延伸むらや延伸切れの
発生が抑制でき高MD延伸倍率でのフィルム連続生産が可
能になる。
After the forced heat shrinkage as described above, if the MD stretching is performed by heating sufficiently at an appropriate temperature, the occurrence of uneven stretching and stretch breakage can be suppressed, and continuous production of the film at a high MD stretching ratio becomes possible. .

本発明に適用する未延伸フィルムとしては、熱可塑性
樹脂に無機充填剤、並びに必要に応じて配合する添加剤
を配合して成形したフィルムが挙げられる。
Examples of the unstretched film applicable to the present invention include a film formed by blending an inorganic filler and an additive to be blended as needed with a thermoplastic resin.

〔実施例〕〔Example〕

以下実施例について説明する。 Hereinafter, embodiments will be described.

実施例1〜5、比較例1〜2 ポリエチレン(三菱油化製LLDPE)100重量部に硫酸バ
リウム粉末150重量部及びステアリン酸カルシウム1.25
重量部を配合した混合物を公知の押出成形機を用いて製
膜し、厚さ300μm、巾250m/mのフィルムを得た。
Examples 1 to 5 and Comparative Examples 1 to 2 100 parts by weight of polyethylene (LLDPE manufactured by Mitsubishi Yuka Co.) were mixed with 150 parts by weight of barium sulfate powder and 1.25 calcium stearate.
The mixture containing the parts by weight was formed into a film using a known extruder to obtain a film having a thickness of 300 μm and a width of 250 m / m.

このフィルムを公知のテンターを用いて95℃に加熱後
TDへ5倍延伸した後、加熱ロールにて第1表に示す温度
とし強制収縮させ、更に公知のロール延伸機を用いて第
1表に示す延伸条件でMD延伸を行い多孔質の延伸フィル
ムを得た。結果を第1表に示す。
After heating this film to 95 ° C using a known tenter
After stretching 5 times to TD, it was forcibly shrunk to the temperature shown in Table 1 with a heating roll, and further MD stretched under a stretching condition shown in Table 1 using a known roll stretching machine to obtain a porous stretched film. Obtained. The results are shown in Table 1.

実施例6〜10、比較例3〜4 ポリプロピレン(三井東圧化学製)100重量部に硫酸
バリウム粉末177重量部及びステアリン酸カルシウム1.2
5重量部を配合した混合物を公知の押出成形機を用いて
製膜し、厚さ300μm、巾250m/mのフィルムを得た。
Examples 6 to 10, Comparative Examples 3 to 4 100 parts by weight of polypropylene (manufactured by Mitsui Toatsu Chemicals), 177 parts by weight of barium sulfate powder and 1.2 parts by weight of calcium stearate
The mixture containing 5 parts by weight was formed into a film using a known extruder to obtain a film having a thickness of 300 μm and a width of 250 m / m.

このフィルムを公知のテンターを用いて120℃に加熱
後TDへ5倍延伸した後、加熱ロールにて第1表に示す温
度とし強制収縮させ、更に公知のロール延伸機を用いて
第1表に示す延伸条件でMD延伸を行い多孔質の延伸フィ
ルムを得た。結果を第1表に示す。
This film was heated to 120 ° C. using a known tenter and stretched 5 times to TD. Then, the film was forcibly shrunk to the temperature shown in Table 1 with a heating roll, and further reduced to Table 1 using a known roll stretching machine. MD stretching was performed under the following stretching conditions to obtain a porous stretched film. The results are shown in Table 1.

〔発明の効果〕 本発明はTD延伸後のMD延伸において発生する延伸切れ
や延伸むら等、従来の技術の欠点を改善し、TD延伸後の
MD延伸でありながら高倍率のTD延伸においても、安定延
伸を行い得る多孔質の延伸フィルム製造方法である。
(Effects of the Invention) The present invention improves the drawbacks of conventional techniques, such as stretch breakage and stretching unevenness occurring in MD stretching after TD stretching, and improves the drawbacks after TD stretching.
This is a method for producing a porous stretched film that can perform stable stretching even in TD stretching at a high magnification while being MD stretching.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】フィルムを流れ方向に対して垂直な方向に
延伸し、更に流れ方向に延伸する多孔質の延伸フィルム
製造方法において、流れ方向に対して垂直な方向に少な
くとも2倍延伸されたフィルムを流れ方向に対して垂直
な方向に10%から50%収縮させた後、流れ方向に延伸す
ることを特徴とする延伸フィルム製造方法。
1. A method for producing a porous stretched film in which a film is stretched in a direction perpendicular to the flow direction and further stretched in the flow direction, wherein the film is stretched at least two times in a direction perpendicular to the flow direction. After shrinking by 10% to 50% in a direction perpendicular to the flow direction, and then stretching the film in the flow direction.
JP1196589A 1989-01-23 1989-01-23 Stretched film manufacturing method Expired - Lifetime JP2618463B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1196589A JP2618463B2 (en) 1989-01-23 1989-01-23 Stretched film manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1196589A JP2618463B2 (en) 1989-01-23 1989-01-23 Stretched film manufacturing method

Publications (2)

Publication Number Publication Date
JPH02194035A JPH02194035A (en) 1990-07-31
JP2618463B2 true JP2618463B2 (en) 1997-06-11

Family

ID=11792331

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1196589A Expired - Lifetime JP2618463B2 (en) 1989-01-23 1989-01-23 Stretched film manufacturing method

Country Status (1)

Country Link
JP (1) JP2618463B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8404340B2 (en) 2005-08-11 2013-03-26 Lynden William Trickey Permeable films

Also Published As

Publication number Publication date
JPH02194035A (en) 1990-07-31

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