JP2732879B2 - Wholly aromatic copolymer polyamide - Google Patents
Wholly aromatic copolymer polyamideInfo
- Publication number
- JP2732879B2 JP2732879B2 JP1011862A JP1186289A JP2732879B2 JP 2732879 B2 JP2732879 B2 JP 2732879B2 JP 1011862 A JP1011862 A JP 1011862A JP 1186289 A JP1186289 A JP 1186289A JP 2732879 B2 JP2732879 B2 JP 2732879B2
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- Japan
- Prior art keywords
- polymerization
- solution
- reaction
- polymer
- wholly aromatic
- Prior art date
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Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は強度,モジュラス等の機械的物性に優れ、耐
熱性,耐薬品性に富んだ新規な全芳香族ポリアミド(以
下アラミドという)に関するものである。さらに詳しく
は有機極性溶媒に可溶なプロセス性の良好な共重合に関
する。The present invention relates to a novel wholly aromatic polyamide (hereinafter, referred to as aramid) having excellent mechanical properties such as strength and modulus, and having high heat resistance and chemical resistance. It is. More specifically, the present invention relates to a copolymer which is soluble in an organic polar solvent and has good processability.
[従来技術] 全芳香族ポリアミドは高強力,高モジュラス及び高い
耐熱性を生かして繊維,フイルム等に幅広く用いられ
る。とりわけパラ型のアラミドであるポリ−p−フェニ
レンテレフタラミド(以下PPTAという)は産業用資材、
保護具等にその特徴を生かしアラミドの主流を成してい
る。[Prior Art] A wholly aromatic polyamide is widely used for fibers, films and the like by utilizing high strength, high modulus and high heat resistance. In particular, para-type aramid poly-p-phenyleneterephthalamide (hereinafter referred to as PPTA) is an industrial material,
Utilizing its features in protective equipment, etc., it is the mainstream of aramid.
然しながらPPTA製造,紡糸成型についてみれば、分子
の剛直性に起因する問題があり、例えば重合反応溶媒と
して生体への毒性が強いヘキサメチルホスホルトリアミ
ドを使用しなければならない。また濃硫酸によって液晶
性の紡糸原液を調製しいわゆる液晶紡糸を行わなければ
ならない。しかも、この硫酸を中和するため大量の中和
剤を必要とし製品中にこれら中和剤から無機イオンが混
入し製品の品質を損なう。又、工程的にも不利である。However, regarding PPTA production and spin molding, there is a problem due to the rigidity of the molecule. For example, hexamethylphosphortriamide, which is highly toxic to living organisms, must be used as a polymerization reaction solvent. In addition, a liquid crystalline spinning solution must be prepared with concentrated sulfuric acid to perform so-called liquid crystal spinning. In addition, a large amount of neutralizing agent is required to neutralize the sulfuric acid, and inorganic ions are mixed into the product from the neutralizing agent, thereby deteriorating the quality of the product. It is also disadvantageous in terms of the process.
これに対して重合溶媒として一般的な有機極性溶媒を
用い等方性紡糸原液を調製しプロセスの簡略化を図る試
みも提案されている。具体的にはエーテル結合を分子鎖
中に共重合し溶解性を改良する方法(例えば、特開昭51
−76386号、特開昭51−134743号、特開昭51−136916
号、特開昭61−252229号、特開昭62−27431号、特開昭6
2−225530号、特開昭62−177022号、特開昭62−177023
号公報等)が数多く提案されている。これらのうちp−
フェニレンジアミン(以下PPDAという)と3,4′−ジア
ミノジフェニルエーテル(以下3,4′−DAPEという)を
共重合した全芳香族共重合ポリアミドは強度,剛性率,
耐薬品性に優れたポリマーであり、一般的な有機極性溶
媒であるN−メチルピロリドン等を重合反応溶媒として
用いることができ、しかもこの重合反応後のポリマー溶
液を直接用いて紡糸等の成型ができプロセスの大幅な改
善が可能となる。On the other hand, an attempt to simplify the process by preparing an isotropic spinning dope using a general organic polar solvent as a polymerization solvent has also been proposed. Specifically, a method of improving the solubility by copolymerizing an ether bond in a molecular chain (for example, Japanese Patent Laid-Open No.
-76386, JP-A-51-134743, JP-A-51-136916
No., JP-A-61-252229, JP-A-62-27431, JP-A-62-27431
2-225530, JP-A-62-177022, JP-A-62-177023
And the like have been proposed. Of these, p-
A wholly aromatic copolymer polyamide obtained by copolymerizing phenylenediamine (hereinafter referred to as PPDA) and 3,4'-diaminodiphenyl ether (hereinafter referred to as 3,4'-DAPE) has strength, rigidity,
It is a polymer with excellent chemical resistance, and N-methylpyrrolidone, which is a common organic polar solvent, can be used as a polymerization reaction solvent. Moreover, molding such as spinning can be directly performed using the polymer solution after the polymerization reaction. The process can be greatly improved.
このような柔軟な結合種であるエーテル結合をポリマ
ー鎖中に導入することは、かかる点で有効な手段である
が、ポリマーの一次構造からも類推できるように耐熱
性,剛性率等の物性で十分な性能を発揮するに至ってい
ない。更に高度の機械的物性、耐熱性を求めた場合、し
かも有機溶媒に可溶で簡便な製造プロセスが採用できる
全芳香族ポリアミドは未だ提供されていないのが現状で
ある。Introducing such a flexible bond, an ether bond, into the polymer chain is an effective means in this respect. However, as can be inferred from the primary structure of the polymer, it is necessary to introduce properties such as heat resistance and rigidity. It has not yet achieved sufficient performance. At present, no wholly aromatic polyamide has been provided yet, which requires a higher degree of mechanical properties and heat resistance, and which is soluble in an organic solvent and can be used in a simple production process.
[発明の構成] 重合反応段階での溶媒への溶解性を維持し、かつより
優れた機械物性を持つ共重合アラミドについて鋭意検討
した結果、従来のPPDA,3,4′−DAPEとテレフタル酸クロ
ライド(以下TPCという)からなる共重合アラミドに対
して、第三のジアミンとして剛直な構造を持つm−トリ
ジンを導入することによって性能が大幅に向上すること
を見いだし本発明に至った。[Constitution of the Invention] As a result of earnestly examining copolymerized aramid having better mechanical properties while maintaining solubility in a solvent at the polymerization reaction stage, conventional PPDA, 3,4'-DAPE and terephthalic acid chloride It has been found that the introduction of m-tolidine having a rigid structure as the third diamine into the copolymerized aramid (hereinafter referred to as TPC) significantly improves the performance, and has led to the present invention.
即ち、本発明は、 テレフタル酸を酸成分とし、m−トリジン(A)、パ
ラフェニレンジアミン(B)及び3,4′−ジアミノジフ
ェニルエーテル(C)をアミン成分とする全芳香族共重
合ポリアミドであって、該アミン成分A、B及びCのモ
ル比が、三角図(図1)で示した範囲HIJKLM内にある全
芳香族共重合ポリアミドである。Aはm−トリジン、B
はパラフェニレンジアミン(PPDA)、Cは3,4′−ジア
ミノジフェニルエーテル(3,4′−DAPE)の成分を示
す。H〜Mの各点はそれぞれ下記組成を示す。That is, the present invention relates to a wholly aromatic copolymer polyamide containing terephthalic acid as an acid component and m-tolidine (A), paraphenylenediamine (B) and 3,4'-diaminodiphenyl ether (C) as amine components. Thus, it is a wholly aromatic copolymer polyamide in which the molar ratio of the amine components A, B and C is within the range HIJKLM shown in the triangular diagram (FIG. 1). A is m-tolidine, B
Represents a component of paraphenylenediamine (PPDA), and C represents a component of 3,4'-diaminodiphenyl ether (3,4'-DAPE). Each point of HM shows the following composition, respectively.
この域を外れた組成では反応溶媒への溶解性が劣り十
分な重合度を持ったポリマーはえられない。また、えら
れたとしても成型物の性能が劣り工業的価値に乏しい。 If the composition is out of this range, the solubility in the reaction solvent is poor and a polymer having a sufficient degree of polymerization cannot be obtained. Moreover, even if it is obtained, the performance of the molded product is inferior and the industrial value is poor.
共重合アラミドを製造する方法としては公知の方法で
ある溶融重合,固相重合,界面重合,溶液重合等があげ
られるが、特に溶液重合法が好ましい。また、反応溶媒
としては一般に公知の有機極性溶媒として知られている
ジメチルホルムアミド,ジメチルアセトアミド,N−メチ
ルピロリドン,N−メチルカプロラクタム,ジメチルスル
ホン,ヘキサメチルホスホルトリアミド,テトラメチル
尿素等から選ばれた少なくとも一種を主成分として用い
ることができる。Examples of the method for producing the copolymerized aramid include known methods such as melt polymerization, solid-phase polymerization, interfacial polymerization, and solution polymerization, and the solution polymerization method is particularly preferred. The reaction solvent is selected from dimethylformamide, dimethylacetamide, N-methylpyrrolidone, N-methylcaprolactam, dimethylsulfone, hexamethylphosphortriamide, tetramethylurea, etc., which are generally known as known organic polar solvents. At least one kind can be used as a main component.
このばあい溶解性を上げるために重合の前,途中、終
了時に公知の無機塩を適当量添加しても差し支えない。
このような塩としては例えば塩化リチウム,塩化カルシ
ュウム等があげられる。また、酸成分とジアミン成分と
の比は実質的に等モルで反応させるが、重合度制御のた
め何れかの成分を過剰に用いることもできる。さらに末
端封鎖剤として単官能性の酸成分、アミン成分を使用し
ても良い。In this case, a known inorganic salt may be added in an appropriate amount before, during, or at the end of the polymerization in order to increase the solubility.
Examples of such salts include lithium chloride and calcium chloride. In addition, the reaction between the acid component and the diamine component is performed in substantially equimolar ratio, but any one of the components can be used in excess for controlling the degree of polymerization. Further, a monofunctional acid component or amine component may be used as a terminal blocking agent.
さらに反応によって生成する塩化水素のごとき酸を捕
束するため脂肪族や芳香族のアミン、第四級アンモニウ
ム塩を併用してもよい。Further, an aliphatic or aromatic amine or a quaternary ammonium salt may be used in combination for capturing an acid such as hydrogen chloride generated by the reaction.
反応の終了後、必要に応じて塩基性の無機化合物たと
えば水酸化ナトリウム,水酸化カリウム,水酸化カルシ
ウム,酸化カルシウム等を添加し中和する。After completion of the reaction, if necessary, a basic inorganic compound such as sodium hydroxide, potassium hydroxide, calcium hydroxide, calcium oxide or the like is added for neutralization.
重合反応において生成するポリマーの溶媒にたいする
濃度は重要である。均質な高重合度のポリマーを得るに
は生成ポリマー濃度として20重量%以下が好ましい。と
りわけ数%から10%の範囲が安定したポリマーを得るの
に好都合である。特に本発明のポリマーは溶液の粘度が
高いので適正なポリマー重合度と溶液濃度に適性化する
必要がある。固有粘度は好ましくは1.5以上10以下、更
に好ましくは2.0以上、8以下が好適である。The concentration of the polymer formed in the polymerization reaction relative to the solvent is important. In order to obtain a homogeneous polymer having a high degree of polymerization, the concentration of the produced polymer is preferably 20% by weight or less. In particular, a range of a few% to 10% is advantageous for obtaining a stable polymer. In particular, since the viscosity of the solution of the polymer of the present invention is high, it is necessary to optimize the degree of polymerization of the polymer and the solution concentration. The intrinsic viscosity is preferably 1.5 or more and 10 or less, more preferably 2.0 or more and 8 or less.
反応条件は特別な制限を必要としない。酸ハライドと
ジアミンとの反応は一般に急速であり、反応温度は例え
ば−25〜100℃好ましくは−10〜80℃である。反応系に
混入する水等、反応を阻害する異物は避けなければなら
ないのは言うまでもない。The reaction conditions do not require any special restrictions. The reaction between the acid halide and the diamine is generally rapid, and the reaction temperature is, for example, -25 to 100C, preferably -10 to 80C. Needless to say, foreign substances that hinder the reaction, such as water mixed in the reaction system, must be avoided.
このようにして得られる共重合アラミドはアルコー
ル、水といった溶媒の中に投入して再沈せしめパルプ状
にして取り出すことができ、これを再度他の溶媒に溶解
して成型に供することができるが重合反応によってえた
溶液をそのまま成型用溶液として用いてもよい。The copolymerized aramid thus obtained can be put into a solvent such as alcohol or water, re-precipitated and taken out in the form of pulp, which can be dissolved again in another solvent and subjected to molding. The solution obtained by the polymerization reaction may be used as it is as a molding solution.
特に本発明の組成での共重合アラミドは溶解性に優れ
たものであり重合反応中にポリマーが析出することがな
いので紡糸等の成型用溶液として直接用いるのが好まし
い。このばあい凝固によって成型物が白化しない条件下
で成型するのが好ましく、そのためには塩化カルシウム
溶液等の無機塩を併用するのが好ましい。Particularly, the copolymerized aramid in the composition of the present invention is excellent in solubility and does not precipitate the polymer during the polymerization reaction. Therefore, it is preferably used directly as a solution for molding such as spinning. In this case, it is preferable to mold under a condition in which the molded product does not whiten due to coagulation, and for that purpose, it is preferable to use an inorganic salt such as a calcium chloride solution in combination.
成型法としては先にのべたパルプ状あるいは粉体状と
したのち圧縮成型する方法、ポリマー溶液の流涎法また
はキャスト法による製膜、湿式法による紡糸、製膜等が
挙げられる。溶液から成型する場合、凝固浴中に押し出
し成型物を一旦固化せしめ次いで水洗延伸,熱処理を行
うことによって繊維,フイルムを得ることができる。こ
のばあい凝固浴として有機極性溶媒/水系が好ましく用
いられる。Examples of the molding method include a method of first forming a solid pulp or a powder and then compression molding, film formation by a salivation method or a cast method of a polymer solution, spinning and film formation by a wet method, and the like. In the case of molding from a solution, fibers and films can be obtained by solidifying the extruded product once in a coagulation bath, followed by washing, drawing and heat treatment. In this case, an organic polar solvent / water system is preferably used as a coagulation bath.
[発明の効果] 本発明はm−トリジンという剛直な骨格を持つ構成単
位をポリマー中に導入することにより、溶媒への溶解性
を維持し、かつ一段と優れた高性能の成型品となりうる
ようにした極めて優れた共重合アラミドである。[Effects of the Invention] In the present invention, by introducing a structural unit having a rigid skeleton called m-tolidine into a polymer, solubility in a solvent can be maintained and a more excellent high-performance molded article can be obtained. It is a very excellent copolymerized aramid.
本発明の共重合アラミドは再沈法,湿式法,ドライジ
ェット法,乾式法等に依って繊維,フイルム,シート,
ハイブリッド等,有用な成型物に加工される。更にはゴ
ム補強材,ロープ,コード,樹脂強化剤として多様な分
野で極めて重要な素材である。The copolymerized aramid of the present invention can be prepared by the following methods: reprecipitation method, wet method, dry jet method, dry method, etc.
Processed into useful molded products such as hybrids. Further, it is a very important material in various fields as a rubber reinforcing material, a rope, a cord, and a resin reinforcing agent.
以下実施例を挙げて本発明をさらに詳細に説明する
が、本発明がこれに限定されないのは言うまでもない。
また実施例でいう部とは重量部をいい、重合度の目安と
なる対数粘度ηinhは98.5重量%の濃硫酸に濃度0.5g/dl
で溶かした溶液を30℃にて通常の方法で測定したもので
ある。Hereinafter, the present invention will be described in more detail with reference to Examples, but it goes without saying that the present invention is not limited thereto.
The term “parts” in the examples means parts by weight, and the logarithmic viscosity ηinh, which is a measure of the degree of polymerization, is 0.5 g / dl in 98.5% by weight of concentrated sulfuric acid.
Was measured at 30 ° C. by an ordinary method.
実施例1 十分に乾燥した攪拌装置着きの三つ口フラスコにNMP1
891.83部、m−トリジン(A)36.358部及びPPDA(B)
13.890部及び3,4′−DAPE(C)35.683部を常温下で添
加し窒素中で溶解した後、攪拌しながらTPC86.926部を
添加した。重合反応の進行に従って粘度は徐々に上昇し
た。最終的に80℃で60分間反応せしめたところ透明性の
極めて優れた粘調なポリマー溶液がえられた。ついでこ
の生成物に22.5重量%の水酸化カルシウムを含有するNM
P139.57部を添加し中和反応を行った。Example 1 NMP1 was placed in a three-necked flask equipped with a sufficiently dried stirrer.
891.83 parts, 36.358 parts of m-tolidine (A) and PPDA (B)
After adding 13.890 parts and 35.683 parts of 3,4'-DAPE (C) at room temperature and dissolving in nitrogen, 86.926 parts of TPC were added with stirring. The viscosity gradually increased with the progress of the polymerization reaction. Finally, when the reaction was carried out at 80 ° C. for 60 minutes, a viscous polymer solution having extremely excellent transparency was obtained. The product is then treated with NM containing 22.5% by weight of calcium hydroxide.
P139.57 parts was added to carry out a neutralization reaction.
得られたポリマー溶液を一部水中にとり析出したポリ
マーを分離したのち乾燥し粘度を測定した結果、ηinh
=4.34であった。A part of the obtained polymer solution was taken in water, and the precipitated polymer was separated and dried, and the viscosity was measured.
= 4.34.
<紡糸> 得られた共重合アラミド溶液を0.17mm*25hのキャッ
プを備えたシリンダーにとり80℃に保ちつつNMP30wt%
の水溶液からなる凝固浴中にエアーギャップ10mmを経由
して押し出した(以下、ドライジェット紡糸という)。
紡糸した糸は水洗,乾燥したのち熱板上、300℃及び520
℃で全延伸倍率20.8で二段延伸し19deのフイラメントを
得た。<Spinning> The obtained copolymerized aramid solution is placed in a cylinder equipped with a cap of 0.17 mm * 25 h and kept at 80 ° C. while keeping NMP at 30 wt%.
(Hereinafter referred to as dry jet spinning) through an air gap of 10 mm into a coagulation bath composed of an aqueous solution of
The spun yarn is washed with water, dried and then placed on a hot plate at 300 ° C and 520 ° C.
The film was stretched in two steps at a total stretching ratio of 20.8 at ℃ to obtain a 19-de filament.
この糸の機械的物性は強度18.3(g/de)、伸度2.1
(%)、モジュラス950(g/de)でありm−トリジンの
ない場合(比較例1)にくらべて大幅に性能が向上し
た。The mechanical properties of this yarn are strength 18.3 (g / de) and elongation 2.1.
(%), The modulus was 950 (g / de), and the performance was significantly improved as compared with the case without m-tolidine (Comparative Example 1).
比較例1 m−トリジンを添加せず重合した共重合アラミドは透
明性の良好なものであった。このNMP溶液を実施例1で
示した方法でドライジェット紡糸して、32de、強度23.2
g/de、伸度3.5%、モジュラス620g/deの糸をえた。Comparative Example 1 The copolymerized aramid polymerized without adding m-tolidine had good transparency. This NMP solution was dry jet-spun by the method described in Example 1 to give a strength of 32de and a strength of 23.2.
A yarn having an elongation of 3.5 g and a modulus of 620 g / de was obtained.
実施例2 m−トリジン60モル%,PPDA20モル%,3,4′−DAPE20
モル%からなるジアミン成分を使用して重合した。即
ち、m−トリジン52.491g、PPDA8.913g、3,4′−DAPE1
6.503gをNMP1895.9中にとり、室温で溶解した後、TPC8
3.665gを攪拌下に添加し、室温で60分、続いて80℃で60
分間重合した。重合の進行とともに粘調になるが反応系
は極めて透明性がよく濁りは全くみとめられなかった。Example 2 60 mol% of m-tolidine, 20 mol% of PPDA, 3,4'-DAPE20
Polymerization was carried out using a diamine component consisting of mol%. That is, m-tolidine 52.491 g, PPDA 8.913 g, 3,4'-DAPE1
Take 6.503 g in NMP1895.9 and dissolve at room temperature, then add TPC8
3.665 g are added with stirring, 60 minutes at room temperature, followed by 60
Polymerized for minutes. The reaction system became viscous as the polymerization progressed, but the reaction system was extremely transparent and no turbidity was observed.
重合反応の後、水酸化カルシウム22.5%を含むNMP溶
液134.337gを徐々に添加し中和反応を終了した。得られ
た溶液はその一部を水により再沈し粘度を測定したとこ
ろηinh=5.63であった。After the polymerization reaction, 134.337 g of an NMP solution containing 22.5% of calcium hydroxide was gradually added to terminate the neutralization reaction. A part of the obtained solution was reprecipitated with water and the viscosity was measured. As a result, ηinh was 5.63.
この溶液を実施例1と同様のドライジェット湿式紡糸
して28デニールの繊維をえた。この糸は強度17.1g/de、
伸度1.9%、モジュラス985g/deの物性を示し強靭な繊維
であった。The solution was subjected to wet jet spinning in the same manner as in Example 1 to obtain fibers of 28 denier. This thread has a strength of 17.1 g / de,
It was a tough fiber showing physical properties of elongation of 1.9% and modulus of 985 g / de.
実施例3 m−トリジン20mol%,PPDA40mol%,3,4′−DAPE40mol
%のジアミン成分を使用して同様に重合した。即ち、m
−トリジン18.916g、PPDA10.271g、3,4′−DAPE35.683g
をNMP1887.44g中にとり常温で溶解したのち急速に攪拌
しながらTPC90.271gを添加した。常温で60分,次いで80
℃に昇温し60分間重合した。得られたポリマーの溶液は
透明性に優れた粘調なものであり粘度はηinh=5.21で
あった。Example 3 20 mol% of m-tolidine, 40 mol% of PPDA, 40 mol of 3,4'-DAPE
% Of the diamine component. That is, m
-Trizine 18.916 g, PPDA 10.271 g, 3,4'-DAPE 35.683 g
Was dissolved in NMP1887.44 g at room temperature, and 90.271 g of TPC was added with rapid stirring. 60 minutes at room temperature, then 80
The temperature was raised to ℃, and polymerization was carried out for 60 minutes. The solution of the obtained polymer was viscous with excellent transparency, and the viscosity was ηinh = 5.21.
この共重合アラミドを実施例1に示した方法によって
製糸化したところ20デニールで強度21.3g/de、伸度2.2
%、モジュラス890g/deであり、m−トリジンの添加に
よって大幅に物性が向上した。This copolymerized aramid was spun into a yarn by the method shown in Example 1 and had a strength of 21.3 g / de and an elongation of 2.2 at 20 denier.
%, The modulus was 890 g / de, and the physical properties were significantly improved by the addition of m-tolidine.
実施例4〜15 次いで組成を各種変更してポリマー溶液の溶解性につ
いて評価した結果を示す。いづれも組成を変更した以外
は、実施例1の方法によった。Examples 4 to 15 Next, the results of evaluating the solubility of the polymer solution by changing the composition in various ways are shown. Except for changing the composition in each case, the method of Example 1 was used.
ポリマーの溶液濁度は重合反応初期及び反応中期に濁
ってくる場合を×で、反応後期で濁るものを△で、又、
濁りがなく透明性の良いものを○で表示した。いずれも
目視によって判定した。評価結果を表1に示した。When the solution turbidity of the polymer becomes cloudy in the early stage and the middle stage of the polymerization reaction, ×, in the late stage of the reaction, Δ,
Good transparency without turbidity was indicated by a circle. All were judged visually. Table 1 shows the evaluation results.
図1はA(m−トリジン)、B(p−フェニレンジアミ
ン)、C(3,4′−ジアミノジフェニルアミン)の3成
分系組成図を示す。三角図中の実線で囲まれた部分は本
発明の特に好ましい範囲である。FIG. 1 shows a three-component composition diagram of A (m-tolidine), B (p-phenylenediamine), and C (3,4'-diaminodiphenylamine). The portion surrounded by the solid line in the triangular diagram is a particularly preferred range of the present invention.
Claims (1)
(A)、パラフェニレンジアミン(B)及び3,4′−ジ
アミノジフェニルエーテル(C)をアミン成分とする全
芳香族共重合ポリアミドであって、該アミン成分A、B
及びCのモル比が、三角図(図1)で示した範囲HIJKLM
内にある全芳香族共重合ポリアミド。1. A wholly aromatic copolymer polyamide comprising terephthalic acid as an acid component and m-tolidine (A), paraphenylenediamine (B) and 3,4'-diaminodiphenyl ether (C) as amine components. , The amine components A and B
And the molar ratio of C are in the range HIJKLM shown in the triangular diagram (FIG. 1).
The wholly aromatic copolymer polyamide inside.
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1011862A JP2732879B2 (en) | 1989-01-23 | 1989-01-23 | Wholly aromatic copolymer polyamide |
US07/428,898 US5006629A (en) | 1988-11-01 | 1989-10-30 | Wholly aromatic polyamide copolymer |
EP89311179A EP0367535B1 (en) | 1988-11-01 | 1989-10-30 | Wholly aromatic polyamide copolymer |
DE68927235T DE68927235T2 (en) | 1988-11-01 | 1989-10-30 | Fully aromatic polyamide copolymer |
DE68921844T DE68921844T2 (en) | 1988-11-01 | 1989-10-30 | Fully aromatic polyamide copolymer. |
EP93101049A EP0541510B1 (en) | 1988-11-01 | 1989-10-30 | Wholly aromatic polyamide copolymer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1011862A JP2732879B2 (en) | 1989-01-23 | 1989-01-23 | Wholly aromatic copolymer polyamide |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02194022A JPH02194022A (en) | 1990-07-31 |
JP2732879B2 true JP2732879B2 (en) | 1998-03-30 |
Family
ID=11789537
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1011862A Expired - Lifetime JP2732879B2 (en) | 1988-11-01 | 1989-01-23 | Wholly aromatic copolymer polyamide |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2732879B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5029003B2 (en) * | 2006-10-17 | 2012-09-19 | 日立化成工業株式会社 | Polyimide resin heat-resistant resin, seamless tubular body, coating film, coating plate and heat-resistant paint using this resin |
JP5277594B2 (en) * | 2007-09-11 | 2013-08-28 | 東レ株式会社 | Aromatic polyamide and aromatic polyamide film |
JP5982851B2 (en) * | 2012-02-14 | 2016-08-31 | 東レ株式会社 | Aromatic polyamide film and method for producing the same |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5176386A (en) * | 1974-12-27 | 1976-07-01 | Teijin Ltd | HOKOZOKU HORIAMIDONOSEIZOHO |
JPS60110918A (en) * | 1983-11-17 | 1985-06-17 | Teijin Ltd | Aromatic copolyamide fiber |
JPS63165515A (en) * | 1986-12-25 | 1988-07-08 | Toray Ind Inc | Aromatic polyamide copolymer fiber |
-
1989
- 1989-01-23 JP JP1011862A patent/JP2732879B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH02194022A (en) | 1990-07-31 |
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