JPS6025457B2 - polyethylene terephthalate film - Google Patents
polyethylene terephthalate filmInfo
- Publication number
- JPS6025457B2 JPS6025457B2 JP52014950A JP1495077A JPS6025457B2 JP S6025457 B2 JPS6025457 B2 JP S6025457B2 JP 52014950 A JP52014950 A JP 52014950A JP 1495077 A JP1495077 A JP 1495077A JP S6025457 B2 JPS6025457 B2 JP S6025457B2
- Authority
- JP
- Japan
- Prior art keywords
- film
- polyethylene terephthalate
- organic compound
- weight
- stretching
- 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
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- Manufacture Of Macromolecular Shaped Articles (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
【発明の詳細な説明】
本発明は製膜性、取扱い性が良好で、且つ、熱劣化に対
して大きな耐性をもつ透明な2軸配向ポリエチレンテレ
フタレートフイルムに関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a transparent biaxially oriented polyethylene terephthalate film that has good film formability and handling properties, and has high resistance to thermal deterioration.
近年、ポリエチレンフタレートフィルムは磁気テープ、
写真、コンデンサ用途などに広く使用されるに至ってい
る。In recent years, polyethylene phthalate film has been used for magnetic tape,
It has come to be widely used in photography, capacitor applications, etc.
しかし、その光輝性、透明性を充分に生かした商品分野
では、その製膜工程、及びフィルム高次加工工程に於て
、滑りが不足したり、熱による劣化をおこすことがあり
、トラブルを生じることが多かった。即ち、滑りが不良
の場合はフィルムを巻いたり、巻戻すことが容易でなく
なり、また高温で使用、加工する際熱劣化し易いものは
機械強度が低下したに、変色、或は透明性の低下を伴う
ため、加工作業が困難になったり、商品価値が低下する
ためである。透明性を要求する分野では55仇m〃の波
長をもつ光線の透過率が少くとも70%好ましくは75
%を越えることが望ましい。フィルムに滑り性を付与す
る技術として従来利用されているものを大別すると、A
二酸化チタン、タルク、カオリナィト、炭酸カルシウ
ム等のポリエチレンテレフタレート合成反応系に不活性
な微粒子を添加する方法。However, in the field of products that take full advantage of its brightness and transparency, troubles may occur during the film forming process and high-level film processing process, such as insufficient slippage or deterioration due to heat. There were many things. In other words, if the slippage is poor, it will not be easy to wind or unwind the film, and if the film is used or processed at high temperatures, it will easily deteriorate due to heat, resulting in decreased mechanical strength, discoloration, or decreased transparency. This is because processing work becomes difficult and product value decreases. In fields requiring transparency, the transmittance of light with a wavelength of 55 m〃 is at least 70%, preferably 75 m.
It is desirable to exceed %. The technologies conventionally used to impart slipperiness to films can be roughly divided into A.
A method of adding inert fine particles to the reaction system for polyethylene terephthalate synthesis such as titanium dioxide, talc, kaolinite, calcium carbonate, etc.
B ポリエチレンテレフタレート合成時に使用する触媒
、着色防止剤等の一部、又は全部を反応の過程で析出せ
しめ、微粒子として存在させる方法。がある。B. A method in which part or all of the catalyst, color inhibitor, etc. used during the synthesis of polyethylene terephthalate is precipitated during the reaction process and is present as fine particles. There is.
また、この他に通常、ポリエチレンテレフタレートでは
用いられないが、ステァリン酸、ステアリン酸亜鉛など
の滑剤を添加する方法も知られている。併し、上記2種
の微粒子を存在させる方法はいずれも微粒子の直径、添
加量コントロールに技術を要する上に、滑り性向上のた
めには粒径を粗く、且つ、多量存在させなければならな
いため、その努力によって逆にフィルムの透明性を低下
せしめるという難を甘受しなければならないのである。In addition, although not normally used with polyethylene terephthalate, a method of adding lubricants such as stearic acid and zinc stearate is also known. However, both methods of making the above two types of fine particles exist require technology to control the diameter of the fine particles and the amount added, and in order to improve slipperiness, the particle size must be coarse and a large amount must be present. However, they must accept the disadvantage that their efforts may actually reduce the transparency of the film.
そこで本発明者らは上記2種の手法を利用するにしても
透明な状態で滑り性良く、乃至、滑り性の改良された、
更に耐熱性良好なポリエチレンテレフタレートフィルム
を得ることが何らかの有機化合物を添加することによっ
て達成できないかを鋭意検討した結果構造式(ここでR
はアルキル基をあらわす)で示される有機化合物を0.
1〜5重量%、好ましくは0.3〜4重量添加混合した
ポリエチレンテレフタレートを2軸に延伸配向させるこ
とによって上記目的、即ち滑り性、耐熱性良好な、55
肌仏の波長をもつ光線の透過率が70%以上であるフィ
ルムとすることができる事を見し、出し本発明に到達し
たものである。Therefore, even if the above two methods are used, the present inventors have found that even if they use the above two methods, they can achieve good or improved slipping properties in a transparent state.
Furthermore, as a result of intensive investigation into whether it was possible to obtain a polyethylene terephthalate film with good heat resistance by adding some kind of organic compound, the structural formula (herein R
represents an alkyl group).
By biaxially stretching and orienting polyethylene terephthalate mixed with 1 to 5% by weight, preferably 0.3 to 4% by weight, 55
It was discovered that a film having a transmittance of 70% or more for light having a wavelength similar to that of the skin can be made, and the present invention was developed based on this finding.
本発明にいうポリエチレンテレフタレートとは繰返し単
位の85%以上がエチレンテレフタレート単位であるよ
うな共重合体、及び15重量%以下のその他のポリマが
混合されている場合を含む。Polyethylene terephthalate as used in the present invention includes copolymers in which 85% or more of the repeating units are ethylene terephthalate units, and cases in which 15% by weight or less of other polymers are mixed.
添加する有機化合物は融点が高いことからもわかるよう
に添加工程、製膜工程で分解、乃至昇華によって揮散す
ることは殆んどない。2鞄配向フィルムは押出機によっ
てポリエチレンテレフタレートを少くとも260午0以
上で溶融押出後、未延伸フィルムなし、次いで2軸に延
伸してつくられるが、該有機化合物はポリエチレンテレ
フタレートとの相潟性が極めて良好であり、その重合工
程及び/又は溶融押出前に添加されるため、少くとも押
出機中で融解して均一に分散されるのである。As can be seen from the fact that the added organic compound has a high melting point, it hardly evaporates due to decomposition or sublimation during the addition process and film forming process. 2. Bag oriented film is made by melt-extruding polyethylene terephthalate using an extruder at a temperature of at least 260 mm or more, followed by biaxial stretching without unstretched film, but the organic compound has compatibility with polyethylene terephthalate. Since it is added before the polymerization process and/or melt extrusion, it melts and is uniformly dispersed at least in the extruder.
例えばポリ塩化ビニルの場合205q0以上に加熱する
と分解が激しく、それよりも高融点の該有機化合物を均
一に混合することは困難である。添加量は0.1重量%
、好ましくは0.箱重量%以上でないと滑り性、耐熱性
共に目的に対して改良効果が不充分であり、また5重量
%、好ましくは4重量%以下であることが、添加により
惹起されるポリエチレンテレフタレートの溶融時の重合
度低下から望ましい。ポリエチレンテレフタレート以外
の樹脂で多用される滑剤、例えばステアリン酸、ステア
リン酸亜鉛、ステアリン酸鉛、流動パラフィン、ステア
リン酸アミド、オレフィン酸アミドなどは融点が低く、
或はフィルムの2輪延伸、又は熱処理工程で発煙したり
、取扱いが難しい場合があり、更に毅膜後のブリード量
コントロールが難しく、経時によってフィルム面が曇っ
て外観不良を生ずることや、溶融押出時の重合度低下が
甚しく生ずる場合があるなど、実質上使用できない。For example, in the case of polyvinyl chloride, heating to 205q0 or higher causes severe decomposition, and it is difficult to uniformly mix the organic compound with a higher melting point than that. Addition amount is 0.1% by weight
, preferably 0. If it is less than 5% by weight, preferably 4% by weight, the effect of improving both slipperiness and heat resistance will be insufficient for the purposes of the polyethylene terephthalate melting caused by the addition. This is desirable because it reduces the degree of polymerization. Lubricants often used in resins other than polyethylene terephthalate, such as stearic acid, zinc stearate, lead stearate, liquid paraffin, stearamide, and olefinic acid amide, have low melting points.
Alternatively, the film may emit smoke or be difficult to handle during the two-wheel stretching or heat treatment process, and it is also difficult to control the amount of bleed after the film is coated, and the film surface may become cloudy over time, resulting in poor appearance. It is practically unusable because the degree of polymerization may be significantly lowered in some cases.
ポリエチレンテレフタレートフィルムでの本発明に於け
る目的の達成は該フィルムが2軸延伸配向され、時によ
り更に熱処理を受けるが、この2軸配向によって、はじ
めて成し遂げられるものであり、未延伸フィルムでは該
化合物が添加されていても滑り性の改良、耐熱性の発現
も全く期待できない点は留意すべきものである。Achievement of the object of the present invention with a polyethylene terephthalate film can only be achieved by biaxially stretching the film and, in some cases, further subjecting it to heat treatment. It should be noted that even if is added, improvement in slipperiness and development of heat resistance cannot be expected at all.
ここでフィルムの滑り性は東洋テスター製スリップテス
ターを用い、ASTMD−189の法に従って測定した
。The slipperiness of the film was measured using a slip tester manufactured by Toyo Tester according to the method of ASTM D-189.
また耐熱性は240℃で1時間、フィルムを熱処理した
後の耐折強さ(耐屈曲回数)であらわした。測定法はJ
ISP8115−63によった(測定温度は室温)。5
5仇h仏の波長をもつ光線の透過率は通常の分光光度計
で測定できる。ポリエチレンテレフタレートの重合度は
オルトクロロフェノール中、25℃で測定した固有粘度
を指標とした。フィルムの延伸条件は特に限定はなく、
2軸に配向していればよく、通常の方法に従えば良いが
、延伸倍率は機械方向に5の音以上、横方向には2.5
〜4.5倍、延伸温度80〜170qoが一般的であり
、熱処理が必要な場合には160〜240こ○が好まし
い。The heat resistance was expressed as the bending strength (number of bending cycles) after the film was heat-treated at 240° C. for 1 hour. The measurement method is J
According to ISP8115-63 (measurement temperature was room temperature). 5
The transmittance of light with a wavelength of 5.5 h can be measured using a conventional spectrophotometer. The degree of polymerization of polyethylene terephthalate was determined by the intrinsic viscosity measured at 25° C. in orthochlorophenol. There are no particular limitations on the stretching conditions for the film.
As long as it is biaxially oriented, the usual method can be followed, but the stretching ratio should be 5 or more in the machine direction and 2.5 in the transverse direction.
-4.5 times and the stretching temperature is generally 80 to 170 qo, and preferably 160 to 240 qo if heat treatment is required.
延伸手法は同時2軸延伸、逐次2軸延伸、これらの組合
せや、或はその後で−鞠方向に再延伸するものを含む。
以下、実施例、比較例で更に詳しく説明する。Stretching techniques include simultaneous biaxial stretching, sequential biaxial stretching, a combination thereof, and subsequent re-stretching in the -marginal direction.
This will be explained in more detail below using Examples and Comparative Examples.
比較例1〜3実施例 1
テレフタル酸80重量部、エチレングリコール42重量
部をオートクレープ中に仕込み、触媒無添加のまま22
0qo、1.5kg/地の加圧条件にて直接ェステル化
反応を行なった。Comparative Examples 1 to 3 Example 1 80 parts by weight of terephthalic acid and 42 parts by weight of ethylene glycol were charged into an autoclave, and the mixture was heated for 22 hours without adding any catalyst.
Direct esterification reaction was carried out under pressurized conditions of 0 qo and 1.5 kg/kg.
留出水は連続的に系外に蟹出せしめ、途中で系の反応率
が50%に達した時点で系内圧力を放圧し始め、最終的
には245qoの常圧下となし、ェステル化反応を終了
した。次いで乾式法酸化ケイ素をエチレングリコールと
水の混合溶液に分散させたスラリ−とし、水酸化テトラ
エチルアンモニウムを添加して餌を調整したスラリーを
ェステル交換反応生成物に添加した。さらに酢酸マグネ
シウム4水和物0.06重量部、三酸化アンチモン0.
0乳重量部、トリメチルホスフェート0.025重量部
を添加した後、常法によって軍縮合を行ない、酸化ケイ
素を0.07%含むポリエチレンテレフタレート(固有
粘度0.625)を得た。このポリエチレンテレフタレ
ートを粉砕し、次の化学構造式を有する有機化合物(融
点230
℃)を夫々2%ブレンドした後、280℃で溶融押出し
法により禾延伸フィルムを作り、続いて9ぴ○で1鞄方
向に3.3倍延伸した後、該方向と直角な方向に3.3
音延伸した。The distilled water was continuously drained out of the system, and when the reaction rate of the system reached 50%, the pressure inside the system started to be released, and finally the pressure was reduced to 245 qo, and the esterification reaction started. has ended. Next, dry process silicon oxide was dispersed in a mixed solution of ethylene glycol and water to form a slurry, and tetraethylammonium hydroxide was added to adjust the bait, and the slurry was added to the transesterification reaction product. Furthermore, 0.06 parts by weight of magnesium acetate tetrahydrate, 0.06 parts by weight of magnesium acetate tetrahydrate, and 0.06 parts by weight of magnesium acetate tetrahydrate.
After adding 0 part by weight of milk and 0.025 part by weight of trimethyl phosphate, military condensation was carried out by a conventional method to obtain polyethylene terephthalate (intrinsic viscosity 0.625) containing 0.07% silicon oxide. This polyethylene terephthalate was crushed and blended with 2% of each organic compound having the following chemical structure (melting point: 230°C), then a stretched film was made by melt extrusion at 280°C, and then one bag was made by 9 pi○. After stretching 3.3 times in the direction, stretching 3.3 times in the direction perpendicular to the direction.
The sound was extended.
次いで、21ぴ○で熱処理して得たフィルム(厚さ10
0山)の特性を調べた結果を次表に示す。尚、勉膜T程
での有機化合物の分解、昇華は殆んど認められず、順調
にフィルムを得ることができた。比較のため、同じ処方
ではあるが、該有機化合物を含まない2軸延伸フィルム
と未延伸フィルム、また該有内機化合物を含む未延伸フ
ィルム(いずれも厚み100ム)をつくり、測定した物
性を同表に記載した。比較例 4〜5
実施例 2〜6
実施例1と同じやり方で、加える有機化合物の濃度を変
えてつくった2軸延伸ポリエチレンテレフタレートフィ
ルム(#25)(但し、熱処理温度が200oo)の勤
摩擦係数、及び固有粘度を次表に示す。Next, a film (thickness 10
The following table shows the results of investigating the characteristics of 0 mountain). Incidentally, almost no decomposition or sublimation of the organic compound was observed during the test film T, and a film could be obtained smoothly. For comparison, we made a biaxially stretched film and an unstretched film that did not contain the organic compound, and an unstretched film that contained the organic compound (each 100 μm thick) with the same formulation, and measured the physical properties. It is listed in the same table. Comparative Examples 4 to 5 Examples 2 to 6 Coefficient of friction of biaxially stretched polyethylene terephthalate film (#25) produced in the same manner as in Example 1 by changing the concentration of the organic compound added (however, the heat treatment temperature was 200 oo) , and intrinsic viscosity are shown in the table below.
固有粘度が0.5未満ではフィルム特性が不良で使用し
難いので、本発明の有機化合物の添加量は5重量%以下
にする必要がある。実施例 7
比較例 6〜9
有機化合物
を1.5%ず
つポリエチレンテレフタレート(固有粘度0.70)ポ
リプロピレン(135℃テトラリン中の固有粘度1.5
4)、A茂樹脂、ポリエチレン(135℃デカリン中の
固有粘度1.48)、ナイロン6の粉末と混合後、次表
に示す条件で溶融押出して未延伸フィルムをつくり、縦
横に2軸延伸した。If the intrinsic viscosity is less than 0.5, the film properties will be poor and it will be difficult to use, so the amount of the organic compound of the present invention added must be 5% by weight or less. Example 7 Comparative Examples 6 to 9 1.5% of each organic compound was added to polyethylene terephthalate (intrinsic viscosity 0.70) polypropylene (intrinsic viscosity 1.5 in tetralin at 135°C)
4) After mixing with Amo resin, polyethylene (intrinsic viscosity 1.48 in decalin at 135°C), and nylon 6 powder, it was melt-extruded under the conditions shown in the following table to make an unstretched film, which was biaxially stretched in the longitudinal and transverse directions. .
ポリエチレンテレフタレート2鞠延伸フィルムは透明で
あったが、ポリプロピレン、ABS樹脂、ポリエチレン
、ナイロン6はいずれも明らかに不透明化するか着色が
甚しくはじめから製品として不適で乃至55仇h#の波
長をもつ光線の透過率が不良であつた。フィルム厚みは
いずれも20〜30ムである。※ 均一な延伸は極めて
困難実施例 8
ィソフタル酸を5%共重合したポリエチレンテレフタレ
ートに次の有機化合物を2.5%濠
合し、280午0に加熱した押出機で溶融押出して未延
伸フィルムをつくり、次いで85qoで、1軸に3.3
倍、これと直角方向に92℃で3.7倍延伸後220℃
で熱処理した。Polyethylene terephthalate 2-layer stretched film was transparent, but polypropylene, ABS resin, polyethylene, and nylon 6 all became clearly opaque or extremely colored, making them unsuitable as products from the beginning or having a wavelength of 55 h#. The light transmittance was poor. The thickness of each film is 20 to 30 mm. * Uniform stretching is extremely difficult Example 8 2.5% of the following organic compound was mixed with polyethylene terephthalate copolymerized with 5% isophthalic acid, and the unstretched film was melt-extruded in an extruder heated to 280:00. Made, then 85qo, 3.3 per axis
220°C after stretching 3.7 times at 92°C in the direction perpendicular to this
heat treated.
得られた厚み50〃の2軸延伸フィルムの波長55仇h
山に於ける光線透過率は83%であり耐熱性の指標であ
る熱処理(24000、1時間)後の耐屈曲回数は該有
機化合物を加えずに同様な手法でつくった2藤延伸フィ
ルムの約1の音大きく、また勤摩擦係数も0.78に対
し0.71と4・ごく、滑り性の改良されたものであっ
た。比較例 10
実施例4と同じやり方で次の化合構造式を有する有機化
合物を2重量%加えてつくった二藤延伸ポリエチレンテ
レフタレートフィルムの動摩擦係数、及び固有粘度を次
表に示す。The wavelength of the obtained biaxially stretched film with a thickness of 50 mm is 55 mm.
The light transmittance of the film is 83%, and the bending resistance after heat treatment (24000, 1 hour), which is an index of heat resistance, is about the same as that of a stretched film made using the same method without adding the organic compound. The sound was louder than that of 1, and the coefficient of friction was 0.71 compared to 0.78, which was 4.0, and the slipperiness was significantly improved. Comparative Example 10 The dynamic friction coefficient and intrinsic viscosity of a Nifuji stretched polyethylene terephthalate film prepared in the same manner as in Example 4 by adding 2% by weight of an organic compound having the following chemical structure are shown in the following table.
実施例4のフィルムよりその固有粘度が著しく低下して
いた。比較例 11
フィルム用の滑剤として知られているステアリン酸と、
耐熱剤として知られている2.6ジ第3ブチルーPーク
レゾール(シェル化学社製、商品名“アィオノール”)
をそれぞれ実施例1と同じやり方で2重量%量添加して
二鞄延伸ポリエチレンテレフタレートフイルム(厚さ1
00仏)をつくった。Its intrinsic viscosity was significantly lower than that of the film of Example 4. Comparative Example 11 Stearic acid, known as a lubricant for films,
2.6-di-tert-butyl-P-cresol (manufactured by Shell Chemical Co., Ltd., trade name "Ionol"), known as a heat resistant agent
were added in an amount of 2% by weight in the same manner as in Example 1 to form two stretched polyethylene terephthalate films (thickness 1
00 Buddha) was created.
このフィルムの特性を調べた結果を次表に示す。ステア
リン酸は著しく固有粘度を低下させた。また2.6ジ第
3ブチル−Pークレゾールは耐熱性に効果がなく、フィ
ルムの透明性を著しく損ねた。比 例 13〜31
実施例と同じ方法で特開昭50−74579号公報の表
1に示されたNo.1〜No.20(M.3は本願発明
で使用の有機化合物で実施例1および比較例2で示した
ので省略)の有機化合物を、ポIJエチレンテレフタレ
ート中にそれぞれ2%加えて未延伸フィルムおよび2軸
延伸フィルムを作り、熱処理前と熱処理後の耐熱性を測
定し、これを下表に示した。The results of investigating the properties of this film are shown in the table below. Stearic acid significantly lowered the intrinsic viscosity. Furthermore, 2.6 di-tert-butyl-P-cresol had no effect on heat resistance and significantly impaired the transparency of the film. Proportions 13 to 31 Using the same method as in Examples, No. 1 shown in Table 1 of JP-A-50-74579 was used. 1~No. 20 (M.3 is an organic compound used in the present invention and is omitted because it was shown in Example 1 and Comparative Example 2) was added in an amount of 2% each to poly-IJ ethylene terephthalate to prepare an unstretched film and a biaxially stretched film. A film was made, and the heat resistance before and after heat treatment was measured, and the results are shown in the table below.
Claims (1)
される有機化合物を0.1〜5重量%含み、かつ2軸方
向に配向されていることを特徴とするポリエチレンテレ
フタレートフイルム。[Claims] 1 (1) Contains 0.1 to 5% by weight of an organic compound represented by the chemical structural formula ▲ Numerical formula, chemical formula, table, etc. ▼ (where R represents a methyl group or ethyl group) A polyethylene terephthalate film characterized in that it is oriented in two axial directions.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52014950A JPS6025457B2 (en) | 1977-02-16 | 1977-02-16 | polyethylene terephthalate film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52014950A JPS6025457B2 (en) | 1977-02-16 | 1977-02-16 | polyethylene terephthalate film |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS53101045A JPS53101045A (en) | 1978-09-04 |
| JPS6025457B2 true JPS6025457B2 (en) | 1985-06-18 |
Family
ID=11875244
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP52014950A Expired JPS6025457B2 (en) | 1977-02-16 | 1977-02-16 | polyethylene terephthalate film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6025457B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59130318A (en) * | 1983-01-17 | 1984-07-26 | Toray Ind Inc | Polyester fiber |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3399237A (en) * | 1964-06-17 | 1968-08-27 | Koppers Co Inc | Ultraviolet light stabilizers for plastic materials |
| JPS5735220B2 (en) * | 1973-11-02 | 1982-07-28 |
-
1977
- 1977-02-16 JP JP52014950A patent/JPS6025457B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS53101045A (en) | 1978-09-04 |
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