JPH0353336B2 - - Google Patents

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Publication number
JPH0353336B2
JPH0353336B2 JP22961986A JP22961986A JPH0353336B2 JP H0353336 B2 JPH0353336 B2 JP H0353336B2 JP 22961986 A JP22961986 A JP 22961986A JP 22961986 A JP22961986 A JP 22961986A JP H0353336 B2 JPH0353336 B2 JP H0353336B2
Authority
JP
Japan
Prior art keywords
film
dope
sulfuric acid
ppta
polymer
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
JP22961986A
Other languages
Japanese (ja)
Other versions
JPS6386731A (en
Inventor
Takenori Taniguchi
Shigemitsu Muraoka
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.)
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry 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 Asahi Chemical Industry Co Ltd filed Critical Asahi Chemical Industry Co Ltd
Priority to JP22961986A priority Critical patent/JPS6386731A/en
Publication of JPS6386731A publication Critical patent/JPS6386731A/en
Publication of JPH0353336B2 publication Critical patent/JPH0353336B2/ja
Granted legal-status Critical Current

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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、ポリパラフエニレンテレフタルアミ
ド(以下、PPTAと称する)から実質的になるフ
イルムの製造法に関する。さらに詳しくは透明で
かつフイルムの長尺方向(以下、MD方向と称
す)および幅方向(以下、TD方向と略す)共に
優れた機械特性を示し、特に超薄膜のPPTAフイ
ルムを得る製造法に関するものである。 (従来の技術) PPTAに代表される直線配位性の芳香族ポリア
ミドは、特に優れた結晶性が高い融点を有し、ま
た剛直な分子構造の故に、耐熱性で高い機械的強
度を有しており、近年、特に注目されている高分
子素材である。また、その光学異方性を示す濃厚
溶液から紡糸された繊維は高い強度及びモジユラ
スを示すことが報告され、既に工業的に実施され
るに至つているが、フイルムへの応用例の提案は
少ない。特公昭57−17886号公報は、PPTA等の
ポリアミドの濃硫酸等を溶媒とする光学異方性ド
ープを加熱により、光学等方化したのち、凝固さ
せ、洗浄・乾燥する方法で、TD・MD方向共に
非常に優れた機械特性を示す透明のフイルムを得
ることに成功しているが、使用するドープが比較
的高濃度であるため超薄膜フイルムを得ることは
非常に困難である。一方、該公報には等方性ドー
プから透明フイルムを得ることが開示されている
が、単に等方性ドープを支持面上に流延したの
ち、凝固・洗浄するだけでは、フイルム中に多量
のボイドが含まれた透明性、機械的性質の双方と
もに不満足なものしか得られない。 また、特公昭57−35088号公報は、PPTA等の
ポリアミドの濃硫酸等を溶媒とする光学異方性ド
ープを環状オリフイスから非凝固性気体中に押出
し、非凝固性気体中に存在する間に、該管状フイ
ルムの内側にガスを圧入して透明なフイルムを得
るとあるが、これら実施例に記載されているよう
な管状オリフイスから凝固浴までの距離が150〜
200mmでは、光学異方性ドープが等方性になるこ
とはなく、不透明の一方向にさけやすい厚手のフ
イルムしか得られない。 (発明が解決しようとする問題点) 本発明の目的は、このような欠点を解消した透
明性に優れ、MD・TD方向共に優れた機械特性
を示す、超薄膜PPTAフイルムの製造法を提供す
ることにある。 (問題点を解決するための手段) すなわち、本発明は、実質的にポリパラフエニ
レンテレフタルアミドと濃硫酸からなる等方性ド
ープを支持面上に流延したのち、凝固・洗浄する
フイルムの製造法において、凝固浴として10℃以
下の20〜70重量%硫酸水溶液を用い、かつ収縮を
制限しつつ乾燥することを特徴とするポリパラフ
エニレンテレフタルアミドフイルムの製造法にあ
る。 本発明の製造方法においては、まず、PPTAか
ら実質的になるポリマーの等方性ドープを調製す
る必要がある。 本発明に用いられるPPTAは実質的に で表されるポリマーであり、従来公知のパラフエ
ニレンジアミンとテレフタロイルクロライドか
ら、低温溶液重合法により製造するのが好都合で
ある。なお、本発明に用いられるポリマーには、
PPTA以外の成分が少量共重合されたり、ブレン
ドされたりしていても、本発明の効果を損なわれ
ない限り、許容される。そのような成分の例とし
て、メタフエニレン、4,4−ビフエニレン、
1,5−ナフタレン、2,6−ナフタレン、4,
4′−ジフエニレンエーテル、3,4′−ジフエニレ
ンエーテル等のポリアミド、ハロゲン、アルキル
基、ニトロ基等で核置換されたPPTAなどが挙げ
られる。 ポリマーは重合度が低いと本発明の目的とする
機械的性質の良好なフイルムが得られなくなるた
め、通常2.5以上、好ましくは3.5以上の対数粘度
ηinh(硫酸100mlにポリマー0.2gを溶解して30℃
で測定した値)を与える重合度のものが選ばれ
る。 本発明のPPTAフイルムの成型に用いるドープ
を調製するのに適した溶媒は、濃硫酸であり、好
ましくは濃度約95重量%以上の硫酸である。硫酸
は濃度100重量%以上のもの、すなわち、発煙硫
酸であつてもよく、またトリハロゲン化酢酸など
を、本発明の効果を損わない範囲で混合して用い
てもよい。 本発明に用いられるドープ中のポリマー濃度
は、常温(約20〜30℃)であり、等方性を示す濃
度のものが好ましく用いられ、具体的には1〜10
重量%、好ましくは2〜6重量%が用いられる。
10重量%以上のポリマー濃度では、異方性を示
し、成型されたフイルムの厚さが厚くなり超薄膜
(例えば3μm以下の厚さ)を作ることが困難であ
る。 一方、あまりに小さいポリマー濃度のドープか
らは実用的な機械的性能のフイルムの取得が困難
である。 本発明において、ドープには普通の添加剤、例
えば、増量剤、除光沢剤、紫外線安定化剤、熱安
定化剤、抗酸化剤、顔料、溶解助剤などを混合し
てもよい。 ドープが、異方性か等方性であるかは、公知の
方法、例えば特公昭50−8474号公報記載の光学的
方法で調べることができるが、その臨界点は、溶
媒の種類、温度、ポリマー濃度、ポリマーの重合
度、非溶媒の含有量等に依存するので、これらの
関係を予め調べることによつて、等方性ドープを
作ることができる。 本発明の方法の特徴は、等方性ドープを支持面
上にフイルム状に流延した後、小さい凝固速度で
凝固される点にあり、凝固浴に、10℃以下の20〜
70重量%の硫酸水溶液を用いる。より好ましく
は、0℃以下の凝固浴である。 このような、凝固浴を用いることによつてフイ
ルムの凝固速度を小さくし、それによつて、フイ
ルム表面でのいわゆるスキン固化層の生成を緩和
して、内部の凝固層との差異を少なくし、フイル
ム全体の均一な凝固収縮を促し、ポリマー濃度が
小しいことに由来する大きな凝固収縮に伴なうボ
イドの生成を抑制することができているものと推
定される。凝固されたフイルムはそのままでは酸
が含まれているため、加熱による機械的物性の低
下の少ないフイルムを製造するためには酸分の洗
浄、除去をできるだけ行う必要がある。酸分の除
去は、具体的には約500ppm以下まで行うことが
望ましく、更に望ましくは200ppm以下である。
洗浄液としては水が通常用いられるが、必要に応
じて温水で行つたり、アルカリ水溶液で中和洗浄
した後、水などで洗浄してもよい。洗浄は、例え
ば洗浄液中でフイルムを走行させたり、洗浄液を
噴霧する等の方法により行われる。 本発明の方法においては、乾燥前後でのフイル
ムの厚み及び面寸法の変化が大きく、この点、高
品質のフイルムの取得のためには乾燥時に特別な
注意が必要である。即ち、皺が生じないように、
緊張下にフイルムの収縮を制限して行う必要があ
る。ここで緊張下というのは、定長下、皺がよら
ない程度に収縮させる、わずかに延伸させるとい
う3つの態様が含まれる。又、乾燥中、もしくは
乾燥前後に延伸を加えることによつて膜厚をより
薄くすることも可能である。 本発明において乾燥とは、空気中、又は窒素、
アルゴンなどの不活性気体雰囲気中で加熱するこ
とであり、加熱ロール上での乾燥、テンターでの
加熱雰囲気での乾燥、シリコーンオイル中での乾
燥、金属枠に固定しての乾燥などのいずれでもよ
い。 乾燥温度は、特に制限されるものではないが、
常温以上または、機械的強度を効果的にするため
には、高温の方が好ましく、100℃以上、さらに
好ましくは200℃以上が用いられる。乾燥の最高
温度は、特に制限されるものではないが、乾燥エ
ネルギーやポリマーの分解性を考慮すれば、500
℃以下が好ましい。 本発明の方法によりフイルムを製造する上で、
上記の工程は、いずれも回分式に行われても連続
的であつてもよく、また全工程を通して連続して
フイルムを走行させつつ製造することも好ましい
実施態様の1つである。また任意の工程で油剤、
識別用の染料などをフイルムに付与してもさしつ
かえない。 (実施例) 以下に実施例および参考例(PPTAの製造例)
を示すが、これらの参考例および実施例は、本発
明を何ら限定するものではない。なお、実施例中
特に規定しない場合は重量部または重量%を示
す。対数粘度ηinhは98%硫酸100mlにポリマー0.2
gを溶解し、30℃で常法で測定した。ドープの粘
度はB型粘度計を用い1rpmの回転速度で測定し
たものである。フイルムの厚さは、直径2mmの測
定面を持つたダイヤルゲージで測定した。強伸度
およびモジユラスは、定速伸長型強伸度測定機に
より、フイルム試料を100mm×10mmの長方形に切
り取り、最初のつかみ長さ30mm、引張り速度30
mm/分で荷重−伸長曲線を5回描き、これにより
算出したものである。次にボイド数は次のように
測定される。適当な大きさのフイルム片を、透過
光を用いた通常の光学顕微鏡により、100倍から
400倍の範囲の倍率で少なくとも異なつた5視野
について観察し、その長径が1μ以上の大きさの
ボイド数を数え、フイルム表面1mm2当たりに換算
する。 参考例 (PPTAの製造) 低温溶液重合法により、次のごとくPPTAを得
た。特公昭53−43986号公報に示された重合装置
中でN−メチルピロリドン1000部に無水塩化リチ
ウム65部を溶解し、次いでパラフエニレンジアミ
ン48.6部を溶解した。8℃に冷却した後、テレフ
タル酸ジクロライド91.4部を粉末状で一度に加え
た。数分後に重合反応物はチーズ状に固化したの
で、特公昭53−43986号公報記載の方法に従つて
重合装置より重合反応物を排出し、直ちに2軸の
密閉型ニーダーに移し、同ニーダー中で重合反応
物を微粉砕した。次に微粉物をヘキシエルミキサ
ー中に移し、ほぼ等量の水を加えさらに粉砕した
後、濾過し数回温水中で洗浄して、110℃の熱風
中で乾燥した。ηinhが5.0の淡黄色のPPTAポリ
マー95部を得た。なお、異なつたηinhのポリマー
は、N−メチルピロリドンとモノマー(パラフエ
ニレンジアミンおよびテレフタル酸ジクロライ
ド)の比、または/およびポリマー間の比等を変
えることによつて容易に得ることができる。 実施例 1 ηinhが5.0のPPTAを99.7重量%の硫酸にポリ
マー濃度3%で溶解し、室温(30℃)で等方性ド
ープを得た。このドープの室温における粘度は
8000ポイズであつた。このドープを減圧脱泡を行
ない、30℃のガラス板上に、0.01mmの段差を有す
るアプリケーターで塗布した。塗布後、0℃、50
%硫酸水溶液中、−10℃の30重量%硫酸水溶液中、
及び−5℃の40重量%硫酸水溶液中にてそれぞれ
凝固させ、中和・水洗を行ない250℃のエアーオ
ーブン中で金属製の枠に固定し乾燥を行なつた。
上記、3つの凝固条件で得られたフイルムの性質
を第1表に示す。なおMDはアプリケーターをひ
いた方向であり、TDはそれと直角の方向であ
る。
(Industrial Application Field) The present invention relates to a method for producing a film consisting essentially of polyparaphenylene terephthalamide (hereinafter referred to as PPTA). More specifically, it relates to a manufacturing method for obtaining an ultra-thin PPTA film that is transparent and exhibits excellent mechanical properties in both the longitudinal direction (hereinafter referred to as the MD direction) and the width direction (hereinafter referred to as the TD direction). It is. (Prior art) Linearly coordinated aromatic polyamides, represented by PPTA, have particularly excellent crystallinity and a high melting point, and due to their rigid molecular structure, they have heat resistance and high mechanical strength. It is a polymer material that has received particular attention in recent years. In addition, it has been reported that fibers spun from concentrated solutions exhibiting optical anisotropy exhibit high strength and modulus, and have already been implemented industrially, but there are few proposals for application to films. . Japanese Patent Publication No. 57-17886 discloses a method in which an optically anisotropic dope of polyamide such as PPTA using concentrated sulfuric acid as a solvent is made optically isotropic by heating, and then coagulated, washed, and dried. Although we have succeeded in obtaining a transparent film that exhibits excellent mechanical properties in both directions, it is extremely difficult to obtain an ultra-thin film due to the relatively high concentration of the dope used. On the other hand, this publication discloses obtaining a transparent film from an isotropic dope, but simply casting the isotropic dope onto a supporting surface, coagulating and washing it will result in a large amount of Only unsatisfactory transparency and mechanical properties including voids can be obtained. In addition, Japanese Patent Publication No. 57-35088 discloses that an optically anisotropic dope of polyamide such as PPTA using concentrated sulfuric acid as a solvent is extruded into a non-coagulable gas through an annular orifice, and while it is in the non-coagulable gas. , it is stated that a transparent film is obtained by pressurizing gas into the inside of the tubular film, but the distance from the tubular orifice to the coagulation bath as described in these examples is 150 ~
At 200 mm, the optically anisotropic dope does not become isotropic, and only a thick film that is opaque and easy to avoid in one direction is obtained. (Problems to be Solved by the Invention) The purpose of the present invention is to provide a method for producing an ultra-thin PPTA film that eliminates these drawbacks, has excellent transparency, and exhibits excellent mechanical properties in both the MD and TD directions. There is a particular thing. (Means for Solving the Problems) That is, the present invention involves casting an isotropic dope consisting essentially of polyparaphenylene terephthalamide and concentrated sulfuric acid onto a supporting surface, and then coagulating and cleaning the film. The method of manufacturing a polyparaphenylene terephthalamide film is characterized by using a 20 to 70% by weight aqueous sulfuric acid solution at 10° C. or lower as a coagulation bath and drying while limiting shrinkage. In the production method of the present invention, it is first necessary to prepare an isotropic polymer dope consisting essentially of PPTA. The PPTA used in the present invention is substantially It is a polymer represented by the formula, and is conveniently produced from conventionally known paraphenylene diamine and terephthaloyl chloride by a low-temperature solution polymerization method. In addition, the polymer used in the present invention includes:
Even if a small amount of components other than PPTA are copolymerized or blended, it is permissible as long as the effects of the present invention are not impaired. Examples of such components include metaphenylene, 4,4-biphenylene,
1,5-naphthalene, 2,6-naphthalene, 4,
Examples include polyamides such as 4'-diphenylene ether and 3,4'-diphenylene ether, and PPTA whose nucleus is substituted with halogen, alkyl group, nitro group, etc. If the polymer has a low degree of polymerization, it will not be possible to obtain a film with good mechanical properties, which is the objective of the present invention. ℃
A polymer with a degree of polymerization that gives a value measured in ) is selected. A suitable solvent for preparing the dope for forming the PPTA film of the present invention is concentrated sulfuric acid, preferably at a concentration of about 95% by weight or more. The sulfuric acid may have a concentration of 100% by weight or more, that is, fuming sulfuric acid, and trihalogenated acetic acid or the like may be used in combination as long as the effects of the present invention are not impaired. The polymer concentration in the dope used in the present invention is at room temperature (approximately 20 to 30°C), and is preferably used at a concentration that exhibits isotropy, specifically 1 to 10
% by weight, preferably 2-6% by weight is used.
At a polymer concentration of 10% by weight or more, the polymer exhibits anisotropy and the thickness of the formed film increases, making it difficult to form an ultra-thin film (for example, a thickness of 3 μm or less). On the other hand, it is difficult to obtain a film with practical mechanical performance from a dope with a too small polymer concentration. In the present invention, the dope may be mixed with common additives, such as fillers, anti-glare agents, UV stabilizers, heat stabilizers, antioxidants, pigments, solubilizing agents, etc. Whether a dope is anisotropic or isotropic can be determined by a known method, such as the optical method described in Japanese Patent Publication No. 50-8474, but the critical point depends on the type of solvent, temperature, Since it depends on the polymer concentration, the degree of polymerization of the polymer, the content of non-solvent, etc., it is possible to prepare an isotropic dope by examining these relationships in advance. The feature of the method of the present invention is that after the isotropic dope is cast in the form of a film on the supporting surface, it is solidified at a low solidification rate.
A 70% by weight aqueous sulfuric acid solution is used. More preferably, it is a coagulation bath of 0° C. or lower. By using such a coagulation bath, the coagulation rate of the film is reduced, thereby relaxing the formation of a so-called skin solidified layer on the film surface, and reducing the difference from the internal solidified layer. It is presumed that uniform coagulation and shrinkage of the entire film is promoted, and the generation of voids due to large coagulation and shrinkage due to the low polymer concentration can be suppressed. Since the solidified film as it is contains acid, it is necessary to wash and remove the acid content as much as possible in order to produce a film whose mechanical properties are less likely to deteriorate due to heating. Specifically, it is desirable to remove the acid content to about 500 ppm or less, more preferably 200 ppm or less.
Water is usually used as the cleaning liquid, but if necessary, warm water may be used, or washing may be performed after neutralization with an alkaline aqueous solution and then with water. Cleaning is performed, for example, by running the film in a cleaning liquid or by spraying the cleaning liquid. In the method of the present invention, the thickness and surface dimensions of the film change significantly before and after drying, and in this respect, special care must be taken during drying in order to obtain a high quality film. In other words, to avoid wrinkles,
It is necessary to limit the contraction of the film under tension. Here, under tension includes three modes: under constant length, contracted to an extent that wrinkles do not form, and slightly stretched. It is also possible to make the film thinner by stretching during drying or before and after drying. In the present invention, drying means drying in air, nitrogen,
It is heating in an inert gas atmosphere such as argon, and can be dried on a heating roll, in a tenter, in a heated atmosphere, in silicone oil, fixed to a metal frame, etc. good. The drying temperature is not particularly limited, but
A temperature higher than normal temperature or a high temperature is preferred in order to effectively improve the mechanical strength, and a temperature higher than 100°C, more preferably higher than 200°C is used. The maximum temperature for drying is not particularly limited, but considering the drying energy and decomposability of the polymer, the maximum temperature is 500°C.
℃ or less is preferable. In producing a film by the method of the present invention,
All of the above steps may be carried out batchwise or continuously, and one preferred embodiment is to manufacture the film while running it continuously throughout the entire process. In addition, oil agent,
It is also possible to add dyes for identification to the film. (Example) Below are examples and reference examples (manufacturing example of PPTA)
However, these reference examples and examples do not limit the present invention in any way. In the examples, parts by weight or weight % are shown unless otherwise specified. Logarithmic viscosity ηinh is 0.2 of polymer in 100ml of 98% sulfuric acid
g was dissolved and measured at 30°C in a conventional manner. The viscosity of the dope was measured using a B-type viscometer at a rotation speed of 1 rpm. The thickness of the film was measured using a dial gauge with a measuring surface of 2 mm in diameter. The strength and elongation and modulus were determined by cutting the film sample into a rectangle of 100 mm x 10 mm using a constant speed extension type strength and elongation measuring machine, with an initial grip length of 30 mm and a tensile speed of 30 mm.
The load-elongation curve was drawn five times in mm/min, and the calculation was made based on this. Next, the number of voids is measured as follows. A piece of film of an appropriate size is magnified from 100x using an ordinary optical microscope using transmitted light.
Observe at least 5 different fields of view at a magnification of 400x, count the number of voids with a major axis of 1 μ or more, and calculate the number of voids per 1 mm 2 of the film surface. Reference Example (Production of PPTA) PPTA was obtained as follows by a low temperature solution polymerization method. In a polymerization apparatus shown in Japanese Patent Publication No. 53-43986, 65 parts of anhydrous lithium chloride was dissolved in 1000 parts of N-methylpyrrolidone, and then 48.6 parts of paraphenylenediamine were dissolved therein. After cooling to 8° C., 91.4 parts of terephthalic acid dichloride was added all at once in powder form. After a few minutes, the polymerization reaction product solidified into a cheese-like shape, so the polymerization reaction product was discharged from the polymerization apparatus according to the method described in Japanese Patent Publication No. 53-43986, and immediately transferred to a twin-screw closed kneader. The polymerization reaction product was finely pulverized. Next, the fine powder was transferred to a Hexiel mixer, and approximately the same amount of water was added thereto for further pulverization, followed by filtration, washing in hot water several times, and drying in hot air at 110°C. 95 parts of pale yellow PPTA polymer with ηinh of 5.0 was obtained. Note that polymers with different ηinh can be easily obtained by changing the ratio of N-methylpyrrolidone and monomers (paraphenylenediamine and terephthalic acid dichloride) and/or the ratio between polymers. Example 1 PPTA having an ηinh of 5.0 was dissolved in 99.7% by weight sulfuric acid at a polymer concentration of 3% to obtain an isotropic dope at room temperature (30°C). The viscosity of this dope at room temperature is
It was 8000 poise. This dope was degassed under reduced pressure and applied onto a glass plate at 30° C. with an applicator having a step of 0.01 mm. After application, 0℃, 50
% sulfuric acid aqueous solution, in a 30 wt % sulfuric acid aqueous solution at -10°C,
and -5°C in a 40% by weight sulfuric acid aqueous solution, neutralized and washed with water, fixed in a metal frame in an air oven at 250°C, and dried.
Table 1 shows the properties of the films obtained under the above three coagulation conditions. Note that MD is the direction in which the applicator is drawn, and TD is the direction perpendicular to it.

【表】 比較例 1 実施例1の減圧脱泡後のドープを30℃のガラス
上に、0.01mmの段差を有するアプリケーターにて
塗布した後、15℃水中、30℃水中、5℃、10重量
%硫酸水溶液中にて凝固させ、中和・水洗を行な
い250℃のエアーオーブン中で金属製の枠に固定
し、乾燥を行なつた。上記条件で得られたフイル
ムの性質を第2表に示す。
[Table] Comparative Example 1 The dope of Example 1 after being degassed under reduced pressure was applied onto glass at 30°C using an applicator with a step of 0.01 mm, and then heated in 15°C water, 30°C water, 5°C, 10 wt. % aqueous sulfuric acid solution, neutralized and washed with water, fixed in a metal frame in an air oven at 250°C, and dried. Table 2 shows the properties of the film obtained under the above conditions.

【表】 実施例 2 ηinhが4.0のPPTAを、99.7重量%の硫酸にポ
リマー濃度5%で溶解し、室温で等方性ドープを
得た。このドープの常温における粘度は12000ポ
イズであつた。製膜し易くするために、ビーカー
に入れ、60℃に保つた。その時もドープは等方性
を示し7000ポイズであつた。このドープを減圧脱
泡を行ない、30℃のガラス板上に、0.01mmの段階
を有するアプリケーターで塗布した。塗布後、−
5℃、40重量%硫酸水溶液中にて凝固させ、中
和・水洗を行ない、250℃のエアーオーブン中で
2軸延伸を行ないながら乾燥を行なつた。上記条
件で得られたフイルムの性質を第3表に示す。
[Table] Example 2 PPTA having an ηinh of 4.0 was dissolved in 99.7% by weight sulfuric acid at a polymer concentration of 5% to obtain an isotropic dope at room temperature. The viscosity of this dope at room temperature was 12,000 poise. To facilitate film formation, it was placed in a beaker and kept at 60°C. At that time, the dope also showed isotropy and had a value of 7000 poise. This dope was degassed under reduced pressure and applied onto a glass plate at 30° C. with an applicator having a step of 0.01 mm. After application, -
It was coagulated in a 40% by weight aqueous sulfuric acid solution at 5°C, neutralized and washed with water, and dried in an air oven at 250°C while being biaxially stretched. Table 3 shows the properties of the film obtained under the above conditions.

【表】 (発明の効果) 本発明の方法で得られるフイルムは高い強度と
高いモジユラスを有するボイドの非常に少ない超
薄手のPPTAフイルムであり、また、高い耐熱
性、高い透明性、高い誘電率を有しているので、
その特徴を活かして、コンデンサー用絶縁体、磁
気テープ用ベースフイルム、熱転写プリンター用
テープなどに特に有用であり、その他包装材、模
型飛行機用の軽量面材、電線被覆材、透過膜等と
しても利用できる。
[Table] (Effects of the invention) The film obtained by the method of the present invention is an ultra-thin PPTA film with very few voids, which has high strength and high modulus, and also has high heat resistance, high transparency, and high dielectric strength. Since it has a rate of
Taking advantage of its characteristics, it is particularly useful for insulators for capacitors, base films for magnetic tapes, tapes for thermal transfer printers, etc. It can also be used as packaging materials, lightweight surface materials for model airplanes, wire covering materials, transparent films, etc. can.

Claims (1)

【特許請求の範囲】[Claims] 1 実質的にポリパラフエニレンテレフタルアミ
ドと濃硫酸からなる等方性ドープを支持面上に流
延したのち、凝固・洗浄するフイルムの製造法に
おいて、凝固浴として10℃以下の20〜70重量%硫
酸水溶液を用い、かつ収縮を制限しつつ乾燥する
ことを特徴とするポリパラフエニレンテレフタル
アミドフイルムの製造法。
1. In a film production method in which an isotropic dope consisting essentially of polyparaphenylene terephthalamide and concentrated sulfuric acid is cast onto a supporting surface, then coagulated and washed, a 20 to 70% by weight bath at 10°C or lower is used as a coagulation bath. 1. A method for producing a polyparaphenylene terephthalamide film, which uses an aqueous solution of 1.5% sulfuric acid and is dried while limiting shrinkage.
JP22961986A 1986-09-30 1986-09-30 Production of poly-p-phenylene terephthalamide film Granted JPS6386731A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22961986A JPS6386731A (en) 1986-09-30 1986-09-30 Production of poly-p-phenylene terephthalamide film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22961986A JPS6386731A (en) 1986-09-30 1986-09-30 Production of poly-p-phenylene terephthalamide film

Publications (2)

Publication Number Publication Date
JPS6386731A JPS6386731A (en) 1988-04-18
JPH0353336B2 true JPH0353336B2 (en) 1991-08-14

Family

ID=16895025

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22961986A Granted JPS6386731A (en) 1986-09-30 1986-09-30 Production of poly-p-phenylene terephthalamide film

Country Status (1)

Country Link
JP (1) JPS6386731A (en)

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US20170301477A1 (en) 2016-04-04 2017-10-19 Capacitor Sciences Incorporated Electro-polarizable compound and capacitor
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