JPS6386731A - Production of poly-p-phenylene terephthalamide film - Google Patents
Production of poly-p-phenylene terephthalamide filmInfo
- Publication number
- JPS6386731A JPS6386731A JP22961986A JP22961986A JPS6386731A JP S6386731 A JPS6386731 A JP S6386731A JP 22961986 A JP22961986 A JP 22961986A JP 22961986 A JP22961986 A JP 22961986A JP S6386731 A JPS6386731 A JP S6386731A
- Authority
- JP
- Japan
- Prior art keywords
- film
- dope
- sulfuric acid
- poly
- drying
- 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.)
- Granted
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 11
- WRDNCFQZLUCIRH-UHFFFAOYSA-N 4-(7-azabicyclo[2.2.1]hepta-1,3,5-triene-7-carbonyl)benzamide Chemical compound C1=CC(C(=O)N)=CC=C1C(=O)N1C2=CC=C1C=C2 WRDNCFQZLUCIRH-UHFFFAOYSA-N 0.000 title abstract 3
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 27
- 238000001035 drying Methods 0.000 claims abstract description 16
- 230000001112 coagulating effect Effects 0.000 claims abstract description 4
- -1 polyparaphenylene terephthalamide Polymers 0.000 claims description 4
- 238000000034 method Methods 0.000 abstract description 13
- 230000015271 coagulation Effects 0.000 abstract description 8
- 238000005345 coagulation Methods 0.000 abstract description 8
- 239000007864 aqueous solution Substances 0.000 abstract description 4
- 239000003990 capacitor Substances 0.000 abstract description 2
- 239000012212 insulator Substances 0.000 abstract description 2
- 125000001140 1,4-phenylene group Chemical group [H]C1=C([H])C([*:2])=C([H])C([H])=C1[*:1] 0.000 abstract 1
- 239000010408 film Substances 0.000 description 45
- 229920000642 polymer Polymers 0.000 description 17
- 229920003366 poly(p-phenylene terephthalamide) Polymers 0.000 description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 239000000243 solution Substances 0.000 description 8
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- 238000006116 polymerization reaction Methods 0.000 description 6
- 239000002904 solvent Substances 0.000 description 6
- 230000003287 optical effect Effects 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000004952 Polyamide Substances 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 239000011521 glass Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- FWFGVMYFCODZRD-UHFFFAOYSA-N oxidanium;hydrogen sulfate Chemical compound O.OS(O)(=O)=O FWFGVMYFCODZRD-UHFFFAOYSA-N 0.000 description 3
- 229920002647 polyamide Polymers 0.000 description 3
- LXEJRKJRKIFVNY-UHFFFAOYSA-N terephthaloyl chloride Chemical compound ClC(=O)C1=CC=C(C(Cl)=O)C=C1 LXEJRKJRKIFVNY-UHFFFAOYSA-N 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000001747 exhibiting effect Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 239000010409 thin film Substances 0.000 description 2
- 230000037303 wrinkles Effects 0.000 description 2
- CBCKQZAAMUWICA-UHFFFAOYSA-N 1,4-phenylenediamine Chemical compound NC1=CC=C(N)C=C1 CBCKQZAAMUWICA-UHFFFAOYSA-N 0.000 description 1
- JZUFKLXOESDKRF-UHFFFAOYSA-N Chlorothiazide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC2=C1NCNS2(=O)=O JZUFKLXOESDKRF-UHFFFAOYSA-N 0.000 description 1
- 239000004606 Fillers/Extenders Substances 0.000 description 1
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 1
- 239000012963 UV stabilizer Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000003712 anti-aging effect Effects 0.000 description 1
- 239000004760 aramid Substances 0.000 description 1
- 229920003235 aromatic polyamide Polymers 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000005034 decoration Methods 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229940050176 methyl chloride Drugs 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 239000002954 polymerization reaction product Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- HIFJUMGIHIZEPX-UHFFFAOYSA-N sulfuric acid;sulfur trioxide Chemical compound O=S(=O)=O.OS(O)(=O)=O HIFJUMGIHIZEPX-UHFFFAOYSA-N 0.000 description 1
- DHCDFWKWKRSZHF-UHFFFAOYSA-N sulfurothioic S-acid Chemical compound OS(O)(=O)=S DHCDFWKWKRSZHF-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、ポリパラフェ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ィルムの製造
法に関する。さらに詳しくは透明でかつフィルムの長尺
方向(以下、MD方向と略す)および暢方向(以下、T
D力方向略す)共に優れた機械特atl−示し、特に超
薄膜のPPTA フィルムを得る製造法に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method for producing a film consisting essentially of polyparaphenylene terephthalamide (hereinafter referred to as PPTA). More specifically, it is transparent, and the longitudinal direction (hereinafter abbreviated as MD direction) and longitudinal direction (hereinafter referred to as T direction) of the film.
The present invention relates to a manufacturing method for obtaining ultra-thin PPTA films, in particular, exhibiting excellent mechanical properties in both directions (D-force direction).
(従来の技術)
PPTAに代我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
度及びモジュラスを示すことが報告され、既に工業的に
実施されるに至っているが、フィ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、光学等力比したのち、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
械特性を示す透明なフィルムを得ることに成功し℃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
ィルムを得ることは非常に困難である。一方、該公報は
等方性ドープから透明フィ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、フィルム中に多閂のざイドが
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。(Prior art) Linear aromatic polyamides, such as 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. Furthermore, it has been reported that fibers spun from a concentrated solution exhibiting optical anisotropy exhibit high strength and modulus, and although this has already been implemented industrially, there are few proposals for its application to films. Special Publication No. 57-17886 is PPTA
This method shows extremely excellent mechanical properties in both the TD and MD directions by heating an optically anisotropic dope made of polyamide such as polyamide using concentrated sulfuric acid as a solvent, performing optical isotropy, coagulating, washing and drying. Although transparent films have been successfully obtained, it is very difficult to obtain ultra-thin films 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 after simply casting the isotropic dope onto a supporting surface,
Simply coagulating and washing the film results in a film that is unsatisfactory in both transparency and mechanical properties as it contains multi-barrel zide.
f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
環状オリフィ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、it状フィルムの内側にガスを
圧入して透明なフィ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ィスから凝固浴まで
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
厚手のフィルムしか得られない。Furthermore, 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 the dope is present in the non-coagulable gas. , it is stated that a transparent film is obtained by pressurizing gas into the inside of an IT-shaped film, but when the distance from the tubular orifice to the coagulation bath is 150 to 200 mm as described in these examples, the optical anisotropy The dope is never isotropic and only a thick film that is opaque and easy to avoid in one direction is obtained.
(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フィルムの!B造法を提供することにある。(Problems to be Solved by the Invention) The object of the present invention is to create an ultra-thin PPTA film that eliminates these drawbacks, has excellent transparency, and exhibits excellent mechanical properties in both the MD and TD directions. Our goal is to provide the B manufacturing method.
(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7エ二レンテレ
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・洗浄するフィルムの製造法にお
いて、凝固浴として106C以下の20〜70!量チ硫
酸水浴液を用い、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ェニレンテレフタルアミドフィル
ムの製造法にある。(Means for Solving the Problems) That is, the present invention provides a film in which an isotropic dope consisting essentially of polypara-7-ethylene terephthalamide and concentrated sulfuric acid is cast onto a supporting surface, and then coagulated and washed. In the manufacturing method, the coagulation bath is 20-70! of 106C or less! The present invention provides a method for producing a polyparaphenylene terephthalamide film, which is characterized by using a sulfuric acid water bath solution and drying while limiting shrinkage.
本発明の製造方法においては、まず、PPTAの等方性
ドープを調製する必要がある。In the manufacturing method of the present invention, it is first necessary to prepare an isotropic dope of PPTA.
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、従来公知のパラフェニレンシアミンとテレ
フタロイルクロライドから、低@浴液重合法により製造
するのが好都合である。PPTA used in the present invention is a polymer substantially represented by, and is conveniently produced from conventionally known paraphenylenecyamine and terephthaloyl chloride by a low @ bath liquid polymerization method.
ポリマーは重合度が低いと本発明の目面とする機械的性
質の良好なフィルムが得られなくなるため、通常2.5
以上、好ましくは6.5以上の対数粘度ηinh (J
A酸100!Llにポリマー肌29を溶解して60℃で
測定した値)を与える重合度のものが選ばれる。If the degree of polymerization of the polymer is low, it will not be possible to obtain a film with good mechanical properties, which is an aspect of the present invention.
Logarithmic viscosity ηinh (J
A acid 100! A polymer having a degree of polymerization that gives a value measured at 60° C. by dissolving polymer skin 29 in Ll is selected.
本発明のPPTAフィ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、好筐しくけ濃度
約95重i%以上の硫酸である。硫酸は濃度100亘量
%以上のもの、すなわち、発煙硫酸であってもよく、筐
たトリノ・ロケ9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。A suitable solvent for preparing the dope used for forming the PPTA film of the present invention is concentrated sulfuric acid, preferably sulfuric acid with 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 may be used in combination with acetic acid such as Torino Roque 9onated acetic acid to the extent that it does not impair the effects of the present invention. .
不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 ’C)であり、等方性を示す濃度のもの
が好筐しく用いられ、具体的には1〜10!Jfチ、好
!しくけ2〜6重斂チが用いられる。10m景チ以上の
ポリマー濃度では、異方性を示し、成型されたフィルム
の厚さが厚くなり超薄膜(例えは6μm以下の厚さ)を
作ることが困難である。The polymer concentration in the dope used in the invention is at room temperature (
(approximately 20 to 30'C), and a concentration that exhibits isotropy is preferably used, specifically 1 to 10! Jf Chi, good! Shikke 2 to 6-jyu-chi is used. At a polymer concentration of 10 μm or more, the polymer exhibits anisotropy and the formed film becomes thick, making it difficult to form an ultra-thin film (for example, a thickness of 6 μm or less).
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@械的a能のフィルムの取得が困難である。On the other hand, it is difficult to obtain a film with practical @mechanical a performance from doping with too small polymer concentration.
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、抗醒化
剤、顔料、溶解助剤などを混入してもよい。In the present invention, the dope may be mixed with common additives, such as extenders, anti-glare agents, UV stabilizers, heat stabilizers, anti-aging agents, pigments, solubilizing agents, etc.
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、非溶媒の官有量等
に依存するので、これらの関係を予め調べることによっ
て、等方性ドープを作ることができる。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, polymerization degree of the polymer, amount of non-solvent, etc., it is possible to prepare an isotropic dope by examining these relationships in advance.
本発明の方法の特徴は、等方性ドープを支持面上にフィ
ルム状に流延した後、小さい凝固速度で凝固させる点に
あり、凝固浴に、10°C以下の20〜70′M量チの
硫酸水浴液を用いる。より好ましくは、0°C以下の凝
固浴である。The method of the present invention is characterized in that the isotropic dope is cast in the form of a film on the support surface and then solidified at a low solidification rate. Use a sulfuric acid water bath solution. More preferably, it is a coagulation bath at 0°C or lower.
このような、凝固浴を用いることによってフィルムの凝
固速度を小さくシ、それによって、フィルム翫面でのい
わゆるスキン固化層の生成を緩和して、内部の凝固層と
の差異を少なくシ、フィルム全体の均一な凝固収縮を促
し、ポリマー濃度が小さ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。凝固されたフィ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
ないフィ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
500 ppm以下まで行うことが望ましく、更に望ま
しくは200 ppm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ったり、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ィルムを走行させたり、
洗浄液を噴錫する等の方法により行われる。By using such a coagulation bath, the coagulation rate of the film can be reduced, thereby alleviating the formation of a so-called skin solidified layer on the film surface, reducing the difference from the internal solidified layer, and reducing the overall film thickness. It is presumed that the formation of voids due to large solidification shrinkage due to the low polymer concentration can be suppressed. Since the coagulated film as it is contains acid, it is necessary to wash and remove the acid 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, and more preferably to 200 ppm or less. Water is usually used as the cleaning liquid, but if necessary, hot water may be used, or washing may be performed by neutralizing with an alkaline aqueous solution and then using water or the like. Cleaning can be done, for example, by running the film in a cleaning solution,
This is done by spraying a cleaning solution or the like.
本発明の方法においては、乾燥前後でのフィルムの厚み
及び面寸法の変化が大きく、この点、高品質のフィルム
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、緊張下にフィルムの収縮を制
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6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って膜厚をより薄くす
ることも可能である。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. That is, it is necessary to limit the shrinkage of the film under tension to prevent wrinkles. Here, under tension includes six modes: under tension, 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.
あり、加熱ロール上での乾燥、テングーでの加熱雰囲気
での乾燥、ソ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。However, any of the following methods may be used: drying on a heated roll, drying in a heated atmosphere with a tengu, drying in soricone oil, drying while fixed to a metal frame, etc.
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、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°C
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°C以下が好ましい。The drying temperature is not particularly limited, but is preferably room temperature or above, and in order to effectively improve mechanical strength, a high temperature is preferable, and is preferably 100°C or above, more preferably 200°C.
The above is used. The maximum temperature for drying is not particularly limited, but in consideration of drying energy and decomposability of the polymer, it is preferably 500°C or less.
本発明の方法によりフィ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ってもよ
く、また全工程を通して連続してフィルムを走行させつ
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ィルムに付与
してもさしつかえない。In producing the film by the method of the present invention, all of the above steps may be performed batchwise or continuously, and the film may be produced while running continuously throughout the entire process. This is one of the preferred embodiments. Further, an oil agent, an identification dye, etc. may be added to the film in any step.
(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″M量部または重量%を示す。(Example) Examples and reference examples (manufacturing examples of PPTA) are shown below, but these reference examples and examples do not limit the present invention in any way. In the examples, unless otherwise specified, "M parts" or "% by weight" are indicated.
対数粘度ηinhは98%硫酸100−にポリマー0.
2 、!i’をFj解し、30°Cで常法で測定した。The logarithmic viscosity ηinh is 98% sulfuric acid 100% and polymer 0.
2,! i' was resolved into Fj and measured at 30°C in a conventional manner.
ドープの粘度はB型粘度計を用いi rpmの回転速度
で測定したものである。フィルムの厚さは、直径2Im
の測定面を持ったダイヤルデージで測定した。The viscosity of the dope was measured using a B-type viscometer at a rotation speed of i rpm. The thickness of the film is 2Im in diameter.
Measurements were made using a dial gauge with a measuring surface.
強伸度およびモジュラスは、定速伸長型強伸度測定機に
より、フィルム試料を100ta×1 ONmの長方形
に切り取り、最初のつかみ長さ50m、引張り速度30
n/分で荷室−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。The strength and elongation and modulus were determined by cutting a film sample into a rectangle of 100ta x 1 ONm using a constant speed extension type strength and elongation measuring machine, with an initial grasp length of 50m and a tensile speed of 30.
The cargo space-extension curve was drawn five times at a rate of n/min, and the calculation was made based on this. Next, the number of voids is measured as follows.
適当な大きさのフィルム片を、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
少なくとも異なった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、フィルム六回1寓
11!2 当たりに換算する。A film piece of an appropriate size is observed in at least 5 different fields of view at a magnification ranging from 100x to 400x using a normal optical microscope using transmitted light, and the number of voids with a major axis of 1 μ or more is determined. Count and convert it to 11!2 per 6 films.
参考例(PPTAの製造) 低温浴液重合法により、次のどと< PPTAを得た。Reference example (manufacture of PPTA) The following PPTA was obtained by a low temperature bath polymerization method.
特公昭53−43986号公報に示された1合装置中で
N−メチルぎクリ2フ1000部に無水塩化リチウム6
5部を溶解し、医いでパラフェニレンシアミン48.6
部を溶解した。8°C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53−4
3986号公報記載の方法に従って重合装置より1合反
応物を排出し、直ちに2軸の密閉型ニーダ−に移し、同
ニーダ−中で1合反応物を微粉砕した。矢に微粉砕物を
へキシエルミキサー中に移し、はぼ等量の水を加えさら
に粉砕した後、1過し数回温水中で洗浄して、110°
Cの熱風中で乾燥した。ηinhが5.0の淡黄色のP
PTAポリマー95部を得た。In a mixing apparatus shown in Japanese Patent Publication No. 53-43986, 6 parts of anhydrous lithium chloride was added to 1000 parts of N-methylchloride.
Dissolve 5 parts and use paraphenylenecyamine 48.6
part was dissolved. After cooling to 8°C, 91.4 parts of terephthalic acid dichloride were added in powder form all at once. After a few minutes, the polymerization reaction product solidified into a cheese-like shape, so the
According to the method described in Japanese Patent No. 3986, the first reaction product was discharged from the polymerization apparatus, immediately transferred to a two-screw closed kneader, and the first reaction product was pulverized in the same kneader. Transfer the finely pulverized material to a hexiel mixer, add an equal amount of water, further pulverize, pass once, wash several times in hot water, and mix at 110°.
It was dried in hot air at C. Pale yellow P with ηinh of 5.0
95 parts of PTA polymer were obtained.
なお、具なったηinhのポリマーは、N−メチルピロ
リドンとモノマー(パラフェ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/およびモノマー
間の比等を変えることによって容易に得ることができる
。In addition, the polymer of ηinh can be easily obtained by changing the ratio of N-methylpyrrolidone and monomers (para-phenylenediamine and terephthalic acid dichloride) and/or the ratio between monomers.
実施例1
ηinhが5.0のPPTAをqq、7重量チの硫酸に
ポリマー濃度6チで溶解し、室温(60°0)で等方性
のドープを得た。このドープの室温における粘度は80
00ボイズであった。このドープを減圧脱泡を行ない、
609Cのがラス板上に、0.01snの段差を有する
アプリケーターで塗布した。塗布後、0°0150%硫
酸水浴液中、−10°Cの60X量チ硫酸水溶液中、及
び−5’Cの40!IIkチ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°Cのエアーオー
ブン中で金属製の枠に固定し乾燥を行なった。上記、6
つの凝固条件で得られたフィルムの性質を第1災に示す
。なおMDはアプリク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。Example 1 PPTA having an ηinh of 5.0 was dissolved in qq, 7 wt sulfuric acid at a polymer concentration of 6 h to obtain an isotropic dope at room temperature (60°0). The viscosity of this dope at room temperature is 80
It was 00 boys. This dope is degassed under reduced pressure,
609C was applied onto a glass plate using an applicator having a step difference of 0.01 sn. After application, 0°0150% sulfuric acid water bath solution, 60X amount of sulfuric acid aqueous solution at -10°C, and 40% at -5'C. Each was coagulated in an aqueous solution of IIk thiosulfuric acid, neutralized and washed with water, fixed in a metal frame in an air oven at 250°C, and dried. Above, 6
The properties of the films obtained under the two coagulation conditions are shown in the first example. Note that MD is the direction of the applicator, and TD is
is the direction perpendicular to it.
比較例1
実施例1の減圧脱泡後のドープを60℃のがラス板上に
、0.01flの段差を有するアプリケーターにて塗布
した後、15°C水中、30°C水中、5’C,10X
量チ硫酸水溶液中にて凝固させ、中和・水洗を行ない2
50°Cのエアーオーブン中で金属製の枠に固定し、乾
燥を行なった。上記条件で得られたフィルムの性質を第
2異に示す。Comparative Example 1 The dope of Example 1 after degassing under reduced pressure was applied onto a glass plate at 60°C with an applicator having a step of 0.01 fl, and then heated in 15°C water, 30°C water, and 5'C ,10X
Coagulate in aqueous sulfuric acid solution, neutralize and wash with water.2
It was fixed in a metal frame and dried in an air oven at 50°C. The properties of the film obtained under the above conditions are shown in the second example.
(以下余白)
実施例2
71nhが4.0のPPTAを、99.7重jlチの硫
酸にポリマー濃度5チで溶解し、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ボイ
ズであった。製膜し易くするために、ビーカーに入れ、
60°0に保った。その時もドープは等方性を示し70
00ボイズであった。このドープを減圧脱泡を行ない、
30℃のガラス板上に、0.01冨冨の段差を有するア
プリケーターで塗布した。塗布後、−5°0140重量
%硫酸水溶液中にて凝固させ、中和・水洗を行ない、2
50℃のエアーオーブン中で2軸延伸を行ないながら乾
燥を行なった。上記条件で得られたフィルムの性質を第
3異に示す。(Left below) Example 2 PPTA having a 71nh of 4.0 was dissolved in 99.7wt sulfuric acid at a polymer concentration of 5t to obtain an isotropic dope at room temperature. The viscosity of this dope at room temperature was 12,000 voids. To make it easier to form a film, put it in a beaker,
It was kept at 60°0. Even then, the dope exhibits isotropy70
It was 00 boys. This dope is degassed under reduced pressure,
It was applied onto a glass plate at 30° C. using an applicator with a step height of 0.01. After coating, coagulate in -5°0140% by weight aqueous sulfuric acid solution, neutralize and wash with water.
Drying was performed while performing biaxial stretching in an air oven at 50°C. The properties of the film obtained under the above conditions are shown in the third example.
(以下余色)
(発明の効果)
本発明の方法で得られるフィルムは高い強度と高いモジ
ュラスを有するボイドの非常に少ない超薄手のPPTA
フィルムであり、また、高い耐熱性、高い透明性、高い
訴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ィルム、熱転写
プリンター用テープなどに特に有用であり、その他色装
材、模型飛行機等用の軽景面材、電線被覆材、透過膜等
としても利用できる。(Hereinafter referred to as extra color) (Effects of the invention) The film obtained by the method of the present invention is an ultra-thin PPTA film with high strength and high modulus and very few voids.
It is a film, and has high heat resistance, high transparency, and high appeal rate, so it is especially useful for insulators for capacitors, base films for magnetic tapes, tapes for thermal transfer printers, etc. In addition, it can also be used as a color decoration material, a light surface material for model airplanes, a wire covering material, a transparent film, etc.
Claims (1)
からなる等方性ドープを支持面上に流延したのち、凝固
・洗浄するフィルムの製造法において、凝固浴として1
0℃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ェ
ニレンテレフタルアミドフィルムの製造法。In a film manufacturing 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, 1 is used as a coagulating bath.
A method for producing a polyparaphenylene terephthalamide film, which comprises using a 20 to 70% by weight aqueous sulfuric acid solution at 0°C or lower and drying while limiting shrinkage.
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 true JPS6386731A (en) | 1988-04-18 |
JPH0353336B2 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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-
1986
- 1986-09-30 JP JP22961986A patent/JPS6386731A/en active Granted
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Also Published As
Publication number | Publication date |
---|---|
JPH0353336B2 (en) | 1991-08-14 |
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