JPS63280618A - Manufacture of chlorotrifluoroethylene polymer film with small water vapor permeability - Google Patents
Manufacture of chlorotrifluoroethylene polymer film with small water vapor permeabilityInfo
- Publication number
- JPS63280618A JPS63280618A JP11538987A JP11538987A JPS63280618A JP S63280618 A JPS63280618 A JP S63280618A JP 11538987 A JP11538987 A JP 11538987A JP 11538987 A JP11538987 A JP 11538987A JP S63280618 A JPS63280618 A JP S63280618A
- Authority
- JP
- Japan
- Prior art keywords
- film
- water vapor
- vapor permeability
- chlorotrifluoroethylene polymer
- rolling
- 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
- UUAGAQFQZIEFAH-UHFFFAOYSA-N chlorotrifluoroethylene Chemical group FC(F)=C(F)Cl UUAGAQFQZIEFAH-UHFFFAOYSA-N 0.000 title claims abstract description 24
- 230000035699 permeability Effects 0.000 title claims abstract description 19
- 229920006254 polymer film Polymers 0.000 title claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 15
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 9
- 238000005096 rolling process Methods 0.000 claims abstract description 23
- 229920000642 polymer Polymers 0.000 claims description 5
- 238000000034 method Methods 0.000 description 5
- 229920002493 poly(chlorotrifluoroethylene) Polymers 0.000 description 5
- 239000005023 polychlorotrifluoroethylene (PCTFE) polymer Substances 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 3
- 238000002834 transmittance Methods 0.000 description 3
- 238000001125 extrusion Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- BQCIDUSAKPWEOX-UHFFFAOYSA-N 1,1-Difluoroethene Chemical compound FC(F)=C BQCIDUSAKPWEOX-UHFFFAOYSA-N 0.000 description 1
- 238000002835 absorbance Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- HCDGVLDPFQMKDK-UHFFFAOYSA-N hexafluoropropylene Chemical group FC(F)=C(F)C(F)(F)F HCDGVLDPFQMKDK-UHFFFAOYSA-N 0.000 description 1
- 239000004973 liquid crystal related substance Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 description 1
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、水蒸気透過性が小さいクロロトリフルオロエ
チレン重合体のフィルムの製法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing a film of chlorotrifluoroethylene polymer having low water vapor permeability.
従来よりクロロトリフルオロエチレン重合体のフィルム
は、水蒸気透過性が小さいことが知られている。そのた
めクロロトリフルオロエチレン重合体のフィルムは、防
湿性が要求される用途に使用されており、例えば、最近
面状発光素子として注目されているエレクトロルミネッ
センス素子(EL素子)において螢光体が水分により劣
化するのを防ぐ封止フィルムとして使用されている。It has been known that chlorotrifluoroethylene polymer films have low water vapor permeability. For this reason, chlorotrifluoroethylene polymer films are used in applications that require moisture resistance.For example, in electroluminescent devices (EL devices), which have recently been attracting attention as planar light emitting devices, phosphors are exposed to moisture. It is used as a sealing film to prevent deterioration.
しかし、EL素子を自動車用の液晶表示のバックライト
等に使用する場合は、従来以上に防湿性が要求され、特
に高温での十分な防湿性が要求される。したがって、封
止フィルムとして使用されるクロロトリフルオロエチレ
ン重合体のフィルムも従来より防湿性の優れたもの、す
なわち水蒸気透過性の小さいものが求められている。ク
ロロトリフルオロエチレン重合体のフィルムの水蒸気透
過性を小さくするには、フィルムの厚さを厚くすること
が考えられるが、フィルムの厚さを厚くすると、透明性
が劣り良好な可視光線透過性が得られず、透明性が要求
される用途では使用できないという問題がある。また、
フィルムの水蒸気透過性を小さくする方法として、フィ
ルムを延伸する方法(特開昭60−96626号公報参
照)やフィルムを熱処理する方法が知られている。しか
し、延伸による方法は、延伸後のフィルムの高温におけ
る寸法安定性が悪く、熱処理による方法は水蒸気透過性
が充分小さくならないという問題点がある。However, when EL elements are used in backlights of liquid crystal displays for automobiles, more moisture resistance is required than ever, and in particular, sufficient moisture resistance at high temperatures is required. Therefore, there has been a demand for films of chlorotrifluoroethylene polymers used as sealing films to have better moisture resistance than ever before, that is, to have low water vapor permeability. In order to reduce the water vapor permeability of a chlorotrifluoroethylene polymer film, it is possible to increase the thickness of the film, but increasing the thickness of the film results in poor transparency and poor visible light transmission. There is a problem in that it cannot be used in applications that require transparency. Also,
As a method of reducing the water vapor permeability of a film, a method of stretching the film (see Japanese Patent Application Laid-Open No. 60-96626) and a method of heat treating the film are known. However, the method using stretching has the problem that the dimensional stability of the stretched film at high temperatures is poor, and the method using heat treatment does not sufficiently reduce water vapor permeability.
本発明の目的は、透明性を損なわずに、従来のものより
水蒸気透過性が小さく、かつ高温における寸法安定性が
優れたクロロトリフルオロエチレン重合体のフィルムを
製造する方法を提供することにある。An object of the present invention is to provide a method for producing a chlorotrifluoroethylene polymer film that has lower water vapor permeability than conventional films and excellent dimensional stability at high temperatures without impairing transparency. .
本発明の要旨は、クロロトリフルオロエチレン重合体の
フィルムを、表面温度が120〜200℃であるロール
で圧延することを特徴とする水蒸気透過性が小さいクロ
ロトリプルオロエチレン重合体のフィルムの製法に存す
る。The gist of the present invention is to provide a method for producing a chlorotrifluoroethylene polymer film with low water vapor permeability, which comprises rolling the chlorotrifluoroethylene polymer film with a roll having a surface temperature of 120 to 200°C. Exists.
本発明において原材料として使用するクロロトリフルオ
ロエチレン重合体のフィルムは、通常押出成形によって
得られる。ここで、クロロトリフルオロエチレン重合体
とはクロロトリフルオロエチレンの単−重合体又はクロ
ロトリフルオロエチレンと30重量%以下の共重合可能
な単量体との共重合体をいう、共重合可能な単量体とし
てはフッ化ビニリデン、テトラフルオロエチレン、ヘキ
サフルオロプロピレン等を例示することができる。The chlorotrifluoroethylene polymer film used as a raw material in the present invention is usually obtained by extrusion molding. Here, the chlorotrifluoroethylene polymer refers to a monopolymer of chlorotrifluoroethylene or a copolymer of chlorotrifluoroethylene and 30% by weight or less of a copolymerizable monomer. Examples of the monomer include vinylidene fluoride, tetrafluoroethylene, and hexafluoropropylene.
本発明において使用する前記フィルムの厚さは、特に限
定されるものではないが通常25〜1000μm、好ま
しくは50〜200Imである。The thickness of the film used in the present invention is not particularly limited, but is usually 25 to 1000 μm, preferably 50 to 200 Im.
圧延処理は、120〜200℃に加熱した2本以上のロ
ール間を通過させることによって行われる。ロール温度
は重要であり、温度が低すぎると十分にかつ均一に圧延
することが難しく、高すぎるとロール表面とフィルムの
剥離性が悪くなる。したがって、ロール温度は120〜
200℃の範囲内にあることが必要であり、特に好まし
くは160〜290℃の範囲である。The rolling treatment is performed by passing the material between two or more rolls heated to 120 to 200°C. The roll temperature is important; if the temperature is too low, it will be difficult to roll the film sufficiently and uniformly, and if it is too high, the peelability between the roll surface and the film will be poor. Therefore, the roll temperature is 120~
It is necessary that the temperature is within the range of 200°C, particularly preferably within the range of 160 to 290°C.
圧延処理に使用するロールは、温度調節が可能なもので
あれば特に制限されることはない、ロールの数は2本以
上であればよく、通常は2〜5本である。ロールの配列
は特に限定されるものではなく、例えば直列形、水平形
、傾斜形、L形、逆り形、Z形等を採用することができ
る。The rolls used in the rolling process are not particularly limited as long as the temperature can be adjusted.The number of rolls may be 2 or more, and is usually 2 to 5 rolls. The arrangement of the rolls is not particularly limited, and for example, a serial type, a horizontal type, an inclined type, an L type, an inverted type, a Z type, etc. can be adopted.
圧延処理におけるロール間隔及びロール回転速度は圧延
処理するフィルムの厚さによって異なるが、圧延処理後
のフィルムの厚さが圧延処理前のフィルムの厚さの80
〜98%、好ましくは85〜95%となるように設定す
ることが好ましい、圧延処理後のフィルムの厚さを圧延
処理前の厚さの80%未満にすると、フィルムに割れ等
が生じて透明性を損なうことがあり、98%をこえる場
合は圧延が不充分だからである。The roll interval and roll rotation speed in the rolling process vary depending on the thickness of the film to be rolled, but the thickness of the film after rolling is 80% of the thickness of the film before rolling.
It is preferable to set the thickness to ~98%, preferably 85 to 95%. If the thickness of the film after rolling is less than 80% of the thickness before rolling, the film will crack and become transparent. This is because rolling is insufficient if it exceeds 98%.
本発明の製法によって製造したクロロトリフルオロエチ
レン重合体のフィルムは、従来のクロロトリフルオロエ
チレン重合体のフィルムに比べ、水蒸気透過性が約20
%前後小さい、これは、圧延処理することによって、フ
ィルムの結晶化度が増大することに起因するものと考え
られる。また、本発明の製法によって製造したクロロト
リフルオロエチレン重合体のフィルムは、高温における
寸法変化率が小さいという特徴がある。The chlorotrifluoroethylene polymer film produced by the production method of the present invention has a water vapor permeability of about 20% compared to conventional chlorotrifluoroethylene polymer films.
This is thought to be due to the fact that the rolling treatment increases the crystallinity of the film. Furthermore, the chlorotrifluoroethylene polymer film produced by the production method of the present invention is characterized by a small dimensional change rate at high temperatures.
以下、実施例及び比較例により本発明を更に詳細に説明
する6
実施例
押出成形によって製造した厚さ200μm、幅300m
mのクロロトリフルオロエチレン重合体フィルム(以下
、PCTFEフィルムと称する)を、直径200關、幅
500Iの2本のロールが直列に配置された直立形ロー
ルカレンダーを使用して、下記の条件で圧延した。Hereinafter, the present invention will be explained in more detail with reference to Examples and Comparative Examples. 6 Example Manufactured by extrusion molding Thickness: 200 μm, Width: 300 m
m of chlorotrifluoroethylene polymer film (hereinafter referred to as PCTFE film) was rolled under the following conditions using an upright roll calender in which two rolls with a diameter of 200 mm and a width of 500 mm were arranged in series. did.
ロール表面温度 190℃
ロール回転数 2 rpm
ロール間隙 30〜40μm(ロール間隙は
予め厚みゲージで実測した値であり、ロールにフィルム
が挿入されることによりロールは上下に動いて間隔は変
化する。)
フィルム引取速度 1.3 m/分分圧後後PCT
FEフィルムについてUンW度、可視光線透過率、寸法
変化率を測定した結果を、圧延前の、PCTFEフィル
ムについての測定結果とあわせて第1表に示す。なお、
・透湿度は、JIS−Z0208に準じ、温度を60℃
にして(JIS−Z 0208は25℃又は40℃)で
測定した。また、寸法変化率は、PCTFEフィルムを
150℃で30分熱処理して、その寸法変化割合を測定
したものである。なお、表中の寸法変化率においてRD
は圧延処理する方向における寸法変化率を、TDは圧延
処理する方向に直角の方向における寸法変化率をそれぞ
れ表している。Roll surface temperature: 190°C Roll rotation speed: 2 rpm Roll gap: 30 to 40 μm (The roll gap is a value measured in advance with a thickness gauge, and as the film is inserted into the roll, the roll moves up and down and the gap changes.) Film take-up speed 1.3 m/min After partial pressure PCT
The results of measuring the UNW degree, visible light transmittance, and dimensional change rate of the FE film are shown in Table 1 together with the measurement results of the PCTFE film before rolling. In addition,
・Moisture permeability is based on JIS-Z0208 at a temperature of 60℃
(JIS-Z 0208 is 25°C or 40°C). Further, the dimensional change rate was determined by heat-treating the PCTFE film at 150° C. for 30 minutes and measuring the dimensional change rate. In addition, in the dimensional change rate in the table, RD
TD represents the dimensional change rate in the rolling direction, and TD represents the dimensional change rate in the direction perpendicular to the rolling direction.
比較例
比較のため、(1)1軸延伸又は (2)熱処理したP
CTFEフィルムを調製し、実施例と同様に測定を行っ
た。なお、フィルムの調製条件は次のとおりである。Comparative Example For comparison, (1) uniaxially stretched or (2) heat-treated P
A CTFE film was prepared and measured in the same manner as in the example. The conditions for preparing the film are as follows.
(1)1軸延伸
延伸温度 :150℃
延伸倍率 ; 4倍
(2)熱処理
熱処理温度 :150℃
熱処理時間 :24時間
測定結果を第1表に示す。ただし、可視光線透過率と透
湿度はフィルムの厚さに依存するので、(a)可視光線
の吸光度はフィルムの厚さに比例する
(b) i3湿度はフィルムの厚さに反比例するとして
フィルムの厚さが200IImにおける換算値を示した
。(1) Uniaxial stretching Stretching temperature: 150°C Stretching ratio: 4 times (2) Heat treatment Heat treatment temperature: 150°C Heat treatment time: 24 hours The measurement results are shown in Table 1. However, since visible light transmittance and moisture permeability depend on the thickness of the film, (a) absorbance of visible light is proportional to the thickness of the film (b) i3 humidity is inversely proportional to the thickness of the film. The converted value is shown when the thickness is 200 IIm.
(以下空白)
第1表に示した結果より、圧延処理後のPCTFEフィ
ルムは、圧延処理前のPCTFEフィルムに比べて、フ
ィルムの厚さが減少しでいるにもかかわらず透湿度が約
20%小さくなっていることがわかる。可視光線透過率
は、圧延処理後においても89%以上を維持しており、
フィルムの透明性は実質上世なわれていないことがわか
る。寸法変化率は、圧延処理する前に比べて、圧延処理
後の方が明らかに小さいことがわかる。これに対して、
比較例の延伸フィルムは寸法変化率が大きく、熱処理フ
ィルムは透湿度の低下が少ないことがわかる。(Blank below) From the results shown in Table 1, the PCTFE film after rolling treatment has a moisture permeability of about 20% compared to the PCTFE film before rolling treatment, even though the thickness of the film is reduced. You can see that it is getting smaller. The visible light transmittance remains at 89% or more even after rolling treatment.
It can be seen that the transparency of the film is virtually unparalleled. It can be seen that the dimensional change rate is clearly smaller after the rolling treatment than before the rolling treatment. On the contrary,
It can be seen that the stretched film of the comparative example has a large dimensional change rate, and the heat-treated film has a small decrease in moisture permeability.
本発明によれば、フィルムの透明性を損なわずに、水蒸
気透過性が小さいクロロトリフルオロエチレン重合体の
フィルムを得ることができる。According to the present invention, a chlorotrifluoroethylene polymer film with low water vapor permeability can be obtained without impairing the transparency of the film.
以上 特許出願人 ダイキン工業株式会社 手続補正書that's all Patent applicant: Daikin Industries, Ltd. Procedural amendment
Claims (1)
表面温度が120〜200℃であるロールで圧延するこ
とを特徴とする水蒸気透過性が小さいクロロトリフルオ
ロエチレン重合体のフィルムの製法。 2、圧延後のフィルムの厚さが圧延前のフィルムの厚さ
に対して80〜98%になるように圧延する特許請求の
範囲第1項記載の水蒸気透過性が小さいクロロトリフル
オロエチレン重合体のフィルムの製法。[Claims] 1. A film of chlorotrifluoroethylene polymer,
A method for producing a chlorotrifluoroethylene polymer film with low water vapor permeability, which comprises rolling with rolls having a surface temperature of 120 to 200°C. 2. The chlorotrifluoroethylene polymer with low water vapor permeability according to claim 1, which is rolled so that the thickness of the film after rolling is 80 to 98% of the thickness of the film before rolling. film manufacturing method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11538987A JPS63280618A (en) | 1987-05-12 | 1987-05-12 | Manufacture of chlorotrifluoroethylene polymer film with small water vapor permeability |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11538987A JPS63280618A (en) | 1987-05-12 | 1987-05-12 | Manufacture of chlorotrifluoroethylene polymer film with small water vapor permeability |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63280618A true JPS63280618A (en) | 1988-11-17 |
Family
ID=14661335
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11538987A Pending JPS63280618A (en) | 1987-05-12 | 1987-05-12 | Manufacture of chlorotrifluoroethylene polymer film with small water vapor permeability |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63280618A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01158047A (en) * | 1987-09-18 | 1989-06-21 | Nitto Denko Corp | Polychlorotrifluoroethylene film, its production and electroluminescence element produced by using said film |
JPH02141224A (en) * | 1988-11-22 | 1990-05-30 | Shin Etsu Chem Co Ltd | Surface protective film |
WO2019203243A1 (en) * | 2018-04-20 | 2019-10-24 | Agc株式会社 | Roll film, method for producing roll film, method for producing copper-clad laminate, and method for producig printed wiring board |
WO2020040023A1 (en) * | 2018-08-24 | 2020-02-27 | Agc株式会社 | Film, film manufacturing method, laminated body, and packaging material |
-
1987
- 1987-05-12 JP JP11538987A patent/JPS63280618A/en active Pending
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01158047A (en) * | 1987-09-18 | 1989-06-21 | Nitto Denko Corp | Polychlorotrifluoroethylene film, its production and electroluminescence element produced by using said film |
JPH0451571B2 (en) * | 1987-09-18 | 1992-08-19 | Nitto Denko Corp | |
JPH02141224A (en) * | 1988-11-22 | 1990-05-30 | Shin Etsu Chem Co Ltd | Surface protective film |
WO2019203243A1 (en) * | 2018-04-20 | 2019-10-24 | Agc株式会社 | Roll film, method for producing roll film, method for producing copper-clad laminate, and method for producig printed wiring board |
US20200407524A1 (en) * | 2018-04-20 | 2020-12-31 | AGC Inc. | Roll film, method for producing roll film, method for producing copper-clad laminate and method for producing printed board |
JPWO2019203243A1 (en) * | 2018-04-20 | 2021-06-10 | Agc株式会社 | Roll film, roll film manufacturing method, copper-clad laminate manufacturing method, and printed circuit board manufacturing method |
WO2020040023A1 (en) * | 2018-08-24 | 2020-02-27 | Agc株式会社 | Film, film manufacturing method, laminated body, and packaging material |
CN112585196A (en) * | 2018-08-24 | 2021-03-30 | Agc株式会社 | Film, method for producing film, laminate, and packaging material |
JPWO2020040023A1 (en) * | 2018-08-24 | 2021-09-24 | Agc株式会社 | Films, film manufacturing methods, laminates and packaging materials |
CN112585196B (en) * | 2018-08-24 | 2023-09-08 | Agc株式会社 | Film, film manufacturing method, laminate, and packaging material |
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