JPS6392434A - Manufacture of thin biaxially stretched film - Google Patents
Manufacture of thin biaxially stretched filmInfo
- Publication number
- JPS6392434A JPS6392434A JP23718386A JP23718386A JPS6392434A JP S6392434 A JPS6392434 A JP S6392434A JP 23718386 A JP23718386 A JP 23718386A JP 23718386 A JP23718386 A JP 23718386A JP S6392434 A JPS6392434 A JP S6392434A
- Authority
- JP
- Japan
- Prior art keywords
- film
- tenter
- thickness
- stretching
- clip
- 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.)
- Pending
Links
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 11
- 229920005992 thermoplastic resin Polymers 0.000 claims abstract description 8
- 238000000034 method Methods 0.000 abstract description 9
- 229920005989 resin Polymers 0.000 abstract description 4
- 239000011347 resin Substances 0.000 abstract description 4
- 230000003247 decreasing effect Effects 0.000 abstract 1
- 239000010408 film Substances 0.000 description 67
- -1 polyethylene terephthalate Polymers 0.000 description 5
- 238000001816 cooling Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229920000139 polyethylene terephthalate Polymers 0.000 description 2
- 239000005020 polyethylene terephthalate Substances 0.000 description 2
- ISPYQTSUDJAMAB-UHFFFAOYSA-N 2-chlorophenol Chemical compound OC1=CC=CC=C1Cl ISPYQTSUDJAMAB-UHFFFAOYSA-N 0.000 description 1
- 229920002292 Nylon 6 Polymers 0.000 description 1
- 229920002302 Nylon 6,6 Polymers 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000009998 heat setting Methods 0.000 description 1
- 229920001903 high density polyethylene Polymers 0.000 description 1
- 239000004700 high-density polyethylene Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229920001707 polybutylene terephthalate Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
Abstract
Description
【発明の詳細な説明】
[技術分野]
本発明は5μm以下の熱可塑性樹脂の二軸延伸フィルム
をテンター法により製造する方法に関するものでおる。DETAILED DESCRIPTION OF THE INVENTION [Technical Field] The present invention relates to a method for producing a biaxially stretched film of thermoplastic resin having a diameter of 5 μm or less by a tenter method.
更に詳しくは、熱可塑性重合体フィルムを幅方向に延伸
する際に、ステンター内におけるフィルムの破断事故を
減少せしめることにより操業性を安定させ、かつ製品と
はならないエツジ部分のロスを減少せしめ、薄い熱可塑
性樹脂の二軸延伸フィルムを安定して製造する方法に関
するものである。More specifically, when stretching a thermoplastic polymer film in the width direction, it stabilizes operability by reducing accidents of film breakage within the stenter, and reduces loss of edge portions that do not become products. The present invention relates to a method for stably producing a biaxially stretched film of thermoplastic resin.
[従来技術とその問題点]
フィルムを幅方向に延伸する際に、極めて薄物ではフィ
ルムエツジ部近傍でのフィルム破断がしばしば発生し、
この破断が操業性を著しく低下させている。また、−度
フイルム破断が発生すると破れ屑の処分、設備の再点検
などのため、製造停止のロス時間が短い場合で数分間、
長い場合には数10分間に及び、しかもダイからの押出
を継続することがあり、樹脂のロスとなる。またこの間
の作業は負1FUが著しいものとなる。フィルム厚さが
薄くなるほど製造工程中の破断事故か多くなり、特に5
μm以下の製膜延伸ではその頻度が大幅に増す。[Prior art and its problems] When stretching a film in the width direction, film breakage often occurs near the film edges for extremely thin films.
This breakage significantly reduces operability. In addition, when film breaks occur, the production stoppage time is short, in some cases for a few minutes, due to disposal of broken debris and re-inspection of equipment.
If it is long, it may take several tens of minutes, and extrusion from the die may continue, resulting in a loss of resin. Also, the work during this time will have a significant negative 1FU. The thinner the film, the more breakage accidents occur during the manufacturing process, especially 5.
The frequency of this phenomenon increases significantly in film forming and stretching of micrometers or less.
フィルムが幅方向の延伸において破断し易い原因の1は
、次にようなテンタークリップの冷却が不充分のためと
推測される。テンターにおいてフィルムの側端部をクリ
ップにより把持して幅方向に延伸し、更にフィルム側端
部をクリップで把持したまま高温で熱処理覆る。クリッ
プはフィルムと共に熱処理の際に高温に曝される。フィ
ルムがテンターからIIfI出されるとき、クリップは
フィルムから離れてテンター人口に戻され、再びフィル
ムを把持して幅方向に延伸する状態を繰返す。ところで
、フィルムの延伸するため把持する位置で、クリップは
延伸温度にまで冷却されておらず、熱処理の際に加熱さ
れた状態から充分に冷却されていない。このとき、クリ
ップが延伸温度より高いと、クリップ把持部のフィルム
が高い温度のクリップにより局部加熱される。テンター
の延伸ゾーンではフィルムの中央部よりもエツジ近傍の
フィルムは高温にあって延伸され易いことになる。One of the reasons why the film tends to break when stretched in the width direction is presumed to be due to insufficient cooling of the tenter clip as described below. In a tenter, the side edges of the film are held with clips and stretched in the width direction, and the film is heat treated at a high temperature while the side edges of the film are held with the clips. The clip, together with the film, is exposed to high temperatures during heat treatment. When the film is taken out from the tenter, the clips are separated from the film and returned to the tenter, and the process of gripping the film again and stretching it in the width direction is repeated. By the way, the clip is not cooled down to the stretching temperature at the position where it is gripped for stretching the film, and is not sufficiently cooled from the state where it was heated during the heat treatment. At this time, if the temperature of the clip is higher than the stretching temperature, the film of the clip gripping portion is locally heated by the high temperature clip. In the stretching zone of the tenter, the film near the edges is at a higher temperature than the center and is more easily stretched.
従って、エツジ近傍が局部的に高倍率に延伸され、その
部分が幼くなりフィルムの破断につながる場合が多い。Therefore, the area near the edge is locally stretched to a high magnification, and that area often becomes young, leading to breakage of the film.
この種の破断はフィルム厚さが薄くなる程多く、これを
防止するためにはフィルムエツジ近傍を厚くするなどの
事前処置を施すものであるが、単にエツジ近傍のフィル
ム厚さは厚(プれば良いというものでなく、限度を超え
てフィルムが厚すぎるとクリップ把持部(=J近に応力
集中か発生し易く、クリップとフィルムとが引かかりや
ずくなったりして、かえって破断じやすくなる。This type of breakage occurs more frequently as the film thickness decreases, and to prevent this, preliminary measures such as thickening the film near the edges are taken, but the thickness of the film near the edges simply changes. However, if the film is too thick beyond the limit, stress concentration tends to occur near the clip gripping part (= J), and the clip and film get caught or become loose, making it more likely to break. .
またフィルム端部を必要以上に厚くすれば当然ロスが大
きくなり経演的にも不利となる。Furthermore, if the end portions of the film are made thicker than necessary, the loss will naturally increase, which will be disadvantageous in terms of performance.
[発明の目的]
本発明は、このような従来技術の問題点に留意し、安定
な、破断の少い条件を種々検問した結束、創意されたも
のである。づなわちテンター法により5μm以下の熱可
塑性樹脂二軸延伸フィルムを製造で−るに際して、フィ
ルムの幅方向の延伸時におけるフィルム破断発生率を少
くでき、かつ製品とはならないエツジ部分のロス量を減
少させることができる薄い熱可塑性樹脂二軸延伸フィル
ムの製造方法を提供することを目的としたものである。[Object of the Invention] The present invention has been devised by taking into account the problems of the prior art and examining various conditions for stable and less likely to break. In other words, when producing biaxially stretched thermoplastic resin films of 5 μm or less using the tenter method, it is possible to reduce the incidence of film breakage during stretching in the width direction of the film, and to reduce the loss of edge portions that do not become products. It is an object of the present invention to provide a method for producing a thin biaxially stretched thermoplastic resin film that can reduce the amount of water used.
[発明の構成1
本発明は、テンター法により5μm以下の熱可塑性樹脂
二軸延伸フィルムを製造するに際して、フィルムの破断
防止のために、テンタークリップ把持部より10mm入
った位置℃のフィルム厚ざ1−1(μm)を、
σC
/× 1 ×−−−−−−−〈 H≦ zxtx5σ[
[士はデンター出]−1のフィルム中央部厚さくμm)
、/は横延伸倍率、σFはテンターのクリップ温度にd
3ける一軸延伸を経た状態の、延伸されるフィルムの降
伏点応力(kMmn+2 ) 、σCはテンターの延伸
温度における縦延伸された状態のフィルムの横延伸での
降伏点応力(kMm…2)]の範囲とするニ、軸延伸フ
ィルム製造方法である。[Configuration 1 of the Invention] The present invention provides a method for manufacturing a biaxially stretched thermoplastic resin film of 5 μm or less by a tenter method, in order to prevent the film from breaking, the thickness of the film is 1° C. at a position 10 mm from the tenter clip gripping portion. −1 (μm), σC /
, / is the transverse stretching ratio, σF is the clip temperature of the tenter d
σC is the yield point stress (kMm...2) of the stretched film after being uniaxially stretched at 3 times, and σC is the yield point stress (kMm...2) of the film stretched longitudinally at the stretching temperature of the tenter in the transverse direction. 2. A method for producing an axially stretched film.
本発明の方法によれば、5μm以下の延伸フィルムを製
造する際、テンターの横延伸においてエツジ近傍でフィ
ルムが破断する頻度が減少する。According to the method of the present invention, when producing a stretched film of 5 μm or less, the frequency of film breakage near the edges during horizontal stretching in a tenter is reduced.
フィルム破断要因としでは、フィルムエツジを把持する
クリップがテンターの横延伸後の工程(熱固定ゾーン)
で高温で加熱され、加熱されたクリップが充分に冷えき
らずに、テンターの人口に戻ってきて、テンター人口の
フィルムを把持し、延伸ゾーンへ進行リ−るとき、クリ
ップか高温なため熱伝導によりクリップ近傍のフィルム
が中央部に較べて高温度に達していて、延伸ゾーンで横
延伸されるとき、この高温度になったフィルムの端の部
分がその中央部よりも容易に延伸されやすく、フィルム
の厚みが極端に薄くなり遂に破断じ到るためである。こ
のクリップ把持部或は近傍におV−Jるフィルムの最適
厚さは、前述のごとく一デンタ部での延伸倍率、クリッ
プ温度及び延伸ゾーン温度におけるフィルムの降伏点応
力に応じて変ってくる。前記の下限条件よりフィルム厚
みが薄い場合には、エツジ近傍が局部的に延伸され、そ
の部分のフィルム厚みが薄くなり、フィルムエツジが裂
けたりする操業上のトラブルが発生するし、逆にフィル
ムエツジ近傍厚みが前記上限条件より厚すぎる場合には
クリップ把持部付近に応力集中が発生し易く、反って破
断し易くなる。また言うまでもなくフィルム端部の捨て
られる部分の樹脂使用料(ロス)が多くなるり過ぎる。The cause of film breakage is that the clip that grips the film edge is in the tenter's lateral stretching process (heat setting zone).
When the heated clip is heated to a high temperature and is not cooled down sufficiently, it returns to the tenter, grips the film in the tenter, and advances to the stretching zone. When the film near the clip reaches a higher temperature than the central part and is laterally stretched in the stretching zone, the high-temperature end parts of the film are more easily stretched than the central part, and the film This is because the thickness becomes extremely thin and eventually breaks. The optimal thickness of the film V-J at or near the clip gripping portion varies depending on the stretching ratio at one denter portion, the clip temperature, and the stress at yield point of the film at the stretching zone temperature, as described above. If the film thickness is thinner than the above lower limit condition, the area near the edge will be stretched locally and the film thickness will become thinner in that area, causing operational troubles such as tearing of the film edge. If the thickness in the vicinity is thicker than the above upper limit condition, stress concentration tends to occur in the vicinity of the clip gripping portion, making it easy to warp and break. Needless to say, too much resin usage (loss) is generated at the discarded end portion of the film.
本発明の製造方法を適用できるフィルムの素材としては
、ポリエチレンテレフタレート、ポリブヂレンテレフタ
レート、ポリエヂレンナフタレンジ力ルポキシレート、
高密度ポリエチレン、ポリプロピレン、ナイロン6、ナ
イロン66等の熱可塑性樹脂があげられる。Film materials to which the production method of the present invention can be applied include polyethylene terephthalate, polybutylene terephthalate, polyethylene naphthalene dipropoxylate,
Examples include thermoplastic resins such as high-density polyethylene, polypropylene, nylon 6, and nylon 66.
以下実施例により本発明を説明する。The present invention will be explained below with reference to Examples.
実施例■及び比較例■(実験番号1〜17)固有粘度0
.60[オルソクロロフェノール、25℃]のポリエチ
レンテレフタレート樹脂を280’Cで溶融し。Tダイ
より40℃の冷却ロール上にキャストし、直ちに冷却し
て未延伸フィルムを造る。この際未延伸フィルム端部と
中央部のフィルム厚さを丁ダイ厚み調整ボルトで調整し
変化させた。Example ■ and Comparative Example ■ (Experiment No. 1 to 17) Intrinsic viscosity 0
.. 60 [orthochlorophenol, 25°C] polyethylene terephthalate resin was melted at 280'C. It is cast onto a cooling roll at 40°C using a T-die and immediately cooled to produce an unstretched film. At this time, the film thickness at the ends and center of the unstretched film was adjusted and varied using a die thickness adjustment bolt.
この未延伸フィルムを長手方向に延伸倍率を3.6倍と
して延伸した後、テンターにより幅(横)延伸し、更に
200°C〜230’Cで熱固定を施した。This unstretched film was stretched in the longitudinal direction at a stretching ratio of 3.6 times, then widthwise (horizontally) stretched using a tenter, and further heat-set at 200°C to 230'C.
表1にその結果を示す。表1の結果よりクリップより1
0mm内側の−のフィルム厚みがそれぞれσC
Z X t X −< H≦zxtx5σF
を満足していないと延伸時にフィルム破断が多発する等
のトラブルが起きることが判った。Table 1 shows the results. From the results in Table 1, 1 from the clip
It has been found that if the film thickness inside 0 mm does not satisfy σC Z X t X −<H≦zxtx5σF, problems such as frequent film breakage occur during stretching.
実施例■
固有粘度0.7のポリエチレン−2,6−ナフタレンジ
カルポキシレートの1.5μm厚さの二軸延伸フィルム
を製造するに際し、第1段延伸を105°Cにおいて3
.9倍の延伸倍率で施し、次いで第二軸方向に122°
Cにて4,1倍延伸し、更に235°Cで熱処理し、毎
分110mで捲取った。このとき、耳端部の厚さが35
μm以上の場合には応力集中に起因するフィルム破断ト
ラブルが発生した。また、テンタークリップを160’
C以下に冷却させないと耳端部の厚さが12μmの場合
に破断が起き易いことも判った。Example ■ When producing a 1.5 μm thick biaxially stretched film of polyethylene-2,6-naphthalene dicarpoxylate with an intrinsic viscosity of 0.7, the first stage stretching was carried out at 105°C for 30 minutes.
.. It was applied at a stretching ratio of 9 times, and then 122° in the second axis direction.
The film was stretched 4.1 times at C, further heat treated at 235°C, and rolled up at 110 m/min. At this time, the thickness of the ear end is 35
When the thickness was .mu.m or more, film breakage problems occurred due to stress concentration. Also, attach the tenter clip to 160'
It was also found that if the thickness of the edge portion was 12 μm, breakage was likely to occur unless the sample was cooled to below C.
[発明の効果]
本発明に依れば、5μm以下の極めて薄い二輪延伸フィ
ルムを安定した操業条件で製造することができる。また
簿いフィルムでは、テンタークリップで把持するフィル
ムの側縁部分をフィルムの中央部分に対して2〜5倍程
度厚くしておくことが、応力集中による破断や、クリッ
プの把持ミスや、博すぎることに起因するフィルム破断
を避は得るものであり、しかも耳端部ロス量を最小限と
なし得る。[Effects of the Invention] According to the present invention, an extremely thin two-wheel stretched film of 5 μm or less can be produced under stable operating conditions. In addition, for bulky film, it is important to make the side edges of the film gripped with tenter clips about 2 to 5 times thicker than the center of the film to prevent breakage due to stress concentration, incorrect gripping of the clips, and excessive curling. This can avoid film breakage caused by this, and furthermore, the amount of edge loss can be minimized.
Claims (1)
ムをテンターにより製造するに際し、テンタークリップ
の把持部より10mmフィルムの中央側に寄った位置に
おけるフィルム厚さH(μm)を、Z×t×σC/σE
<H≦5×Z×t の範囲として、テンターにより延伸することからなる薄
い二軸延伸フィルムの製造方法。 〔但し、tはテンター出口のフィルム中央部の厚さ(μ
m)、Zは横(幅)方向の延伸倍率、σCはテンターの
延伸温度における延伸されるフィルムの降伏点応力(k
g/mm^2)、σEはテンターのクリップ温度におけ
る延伸されるフィルムの降伏点応力(kg/mm^2)
。[Claims] When producing a biaxially stretched film made of thermoplastic resin with a thickness of 5 μm or less using a tenter, the film thickness H (μm) at a position 10 mm closer to the center of the film than the gripping part of the tenter clip. , Z×t×σC/σE
<H≦5×Z×t A method for producing a thin biaxially stretched film comprising stretching with a tenter. [However, t is the thickness of the central part of the film at the exit of the tenter (μ
m), Z is the stretching ratio in the transverse (width) direction, and σC is the yield stress of the stretched film at the stretching temperature of the tenter (k
g/mm^2), σE is the yield stress of the stretched film at the tenter clip temperature (kg/mm^2)
.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23718386A JPS6392434A (en) | 1986-10-07 | 1986-10-07 | Manufacture of thin biaxially stretched film |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23718386A JPS6392434A (en) | 1986-10-07 | 1986-10-07 | Manufacture of thin biaxially stretched film |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6392434A true JPS6392434A (en) | 1988-04-22 |
Family
ID=17011602
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP23718386A Pending JPS6392434A (en) | 1986-10-07 | 1986-10-07 | Manufacture of thin biaxially stretched film |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6392434A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003025424A (en) * | 2001-07-17 | 2003-01-29 | Kuraray Co Ltd | Ethylene/vinyl alcohol copolymer film |
JP2007253517A (en) * | 2006-03-24 | 2007-10-04 | Toyobo Co Ltd | Polymer film manufacturing apparatus and polymer film manufacturing method |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS53146772A (en) * | 1977-05-27 | 1978-12-20 | Unitika Ltd | Production of thin biaxially drawn film of thermoplastic resin |
-
1986
- 1986-10-07 JP JP23718386A patent/JPS6392434A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS53146772A (en) * | 1977-05-27 | 1978-12-20 | Unitika Ltd | Production of thin biaxially drawn film of thermoplastic resin |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003025424A (en) * | 2001-07-17 | 2003-01-29 | Kuraray Co Ltd | Ethylene/vinyl alcohol copolymer film |
JP2007253517A (en) * | 2006-03-24 | 2007-10-04 | Toyobo Co Ltd | Polymer film manufacturing apparatus and polymer film manufacturing method |
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