JPH02269156A - Novel dope for shaping - Google Patents

Novel dope for shaping

Info

Publication number
JPH02269156A
JPH02269156A JP8810089A JP8810089A JPH02269156A JP H02269156 A JPH02269156 A JP H02269156A JP 8810089 A JP8810089 A JP 8810089A JP 8810089 A JP8810089 A JP 8810089A JP H02269156 A JPH02269156 A JP H02269156A
Authority
JP
Japan
Prior art keywords
polyimide
dope
sulfuric acid
acid
concentration
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP8810089A
Other languages
Japanese (ja)
Inventor
Noritsugu Saiki
斎木 紀次
Katsuo Kunugi
功刀 克男
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.)
Teijin Ltd
Original Assignee
Teijin 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 Teijin Ltd filed Critical Teijin Ltd
Priority to JP8810089A priority Critical patent/JPH02269156A/en
Publication of JPH02269156A publication Critical patent/JPH02269156A/en
Pending legal-status Critical Current

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  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Artificial Filaments (AREA)

Abstract

PURPOSE:To provide a shaping dope exhibiting a stream birefringence property and giving polyimide shaped products having excellent heat resistance and mechanical characteristics by dissolving a polyimide having a specific structure in sulfuric acid and/or methane sulfonic acid. CONSTITUTION:(A) Pyromellitic acid (derivative) and 2,2'-dimethylbenzidine (derivative) are reacted with each other at a temperature of <=80 deg.C in a solvent and subsequently heated or treated with an imidizing agent (e.g. acetic anhydride) to prepare a polyimide comprising the structural units of the formula and having an intrinsic viscosity of >=1, preferably >=1.5, (at 35 deg.C, in sulfuric acid), which is dissolved in (B) sulfuric acid (having a concentration of >=98% and containing <=30% of fuming sulfuric acid) and/or methane sulfonic acid to provide a novel shaping dope having a concentration of >=5wt.%, preferably >=8wt.%, and exhibiting a stream birefringence property.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、耐熱性及び力学的性質の優れたポリイミド成
形体、特に繊維、フィルム、パルプ状粒子を製造する際
に有用な成形用原液となり得る流動複屈折性を示す新規
な新規成形用ドープに関する。
Detailed Description of the Invention (Field of Industrial Application) The present invention provides a molding stock solution useful for producing polyimide molded articles with excellent heat resistance and mechanical properties, particularly fibers, films, and pulp-like particles. The present invention relates to a novel molding dope exhibiting flow birefringence.

(従来の技術) 従来、ポリイミドは耐熱性、機械的特性、電気的特性、
耐候性等の優れた繊維、フィルム、その他の成形品の原
料として有用であることが知られている。例えば、4,
4′−ジアミノジフェニルエーテルとピロメリット酸ジ
酸無水物から製造されるポリイミドからは優れた耐熱性
を有するフィルムが得られ、電気絶縁用途等に広く使用
されている。
(Conventional technology) Conventionally, polyimide has excellent heat resistance, mechanical properties, electrical properties,
It is known to be useful as a raw material for fibers, films, and other molded products with excellent weather resistance. For example, 4,
Polyimides produced from 4'-diaminodiphenyl ether and pyromellitic dianhydride provide films with excellent heat resistance and are widely used in electrical insulation applications.

また、耐熱性繊維・フィルムの分野では、アラミド系の
繊維や合成紙、ポリイミド系のフィルム等が使用されて
いるが、宇宙・航空機用途の先端素材の高度化等によつ
゛て、より高い耐熱性と高強力・高モジュラス等の機械
的特性を有するものが近年要求されるようになっている
In addition, in the field of heat-resistant fibers and films, aramid fibers, synthetic papers, polyimide films, etc. are used, but with the advancement of advanced materials for space and aircraft applications, they are becoming more heat-resistant. In recent years, there has been a demand for materials with mechanical properties such as high strength, high strength, and high modulus.

耐熱性繊維の分野でも、近年、比較的剛直な骨格を有す
るポリイミド繊維の報告がなされている。
In the field of heat-resistant fibers, polyimide fibers having relatively rigid skeletons have been reported in recent years.

特公昭57−37687号公報には、ポリアミド酸溶液
を1価、2価もしくは3価アルコールもしくはそれらの
混合物又は極性溶媒の水溶液中に紡出し、得られたゲル
繊維を延伸・乾燥・熱処理することにより、耐炎性で高
強力・高モジュラスの繊維を製造する技術が記載されて
いる。また、繊維学会誌、40、 T−480<198
4+及び特開昭59−157319号公報等には、ポリ
アミド酸の一部をポリイミドに閉環することにより湿式
凝固性の改良された紡糸原液となし、これを同様に湿式
紡糸して得た糸状体を無水酢酸/ピリジン系に浸漬して
イミド化を促進し、乾燥後に熱処理して、さらに力学特
性の優れたポリイミド繊維を得ることが記載されている
。しかしながら、いずれの方法によって得られる繊維も
その力学特性は、高性能繊維として満足できるレベルに
は達していない。これは、−aに剛直骨格を有するポリ
マーで、かつ溶液成形により高度な力学特性を得る場合
、成形用ドープが、ポリ−p−フェニレンテレフタルア
ミドの製造方法に代表されるように流動複屈折性、更に
は光学異方性を示すことが重要な条件となっている。こ
れは、ポリマー分子鎖がドメインと呼ばれる集合体組織
を形成することにより、極めて配向しやすい状態が成形
前に予め作られ、その結果、高度に配向の促進した成形
体を得ることができるからである。剛直骨格ポリイミド
の場合、成形用ポリアミド酸ドープが、流動複屈折性、
更には光学異方性を示すことはないばかりか、最終的に
得られるポリイミドが剛直であっても、その成形用前駆
体であるポリアミド酸は、下記の如く、 (Arは剛直骨格ジアミン残基) (1)のようなp−配向体と(2)のようなm−配向体
とが混在する骨格を持ち、従ってポリマー分子鎖は直線
でなく、折れまがった針金のような状態となる。従って
、成形時の配向促進が困難で、得られる力学特性も満足
な値を示さない。これに対し、特開昭60−65112
号公報等に示される如く、ポリイミド骨格をややフレキ
シブルなものとし、溶媒可溶性のポリイミドを得、これ
を成形することにより高強力繊維を得る方法が提案され
ているが、この場合は骨格がフレキシブルな故、高モジ
ユラス化は達成されない。
Japanese Patent Publication No. 57-37687 discloses that a polyamic acid solution is spun into an aqueous solution of monohydric, dihydric, or trihydric alcohol, a mixture thereof, or a polar solvent, and the resulting gel fiber is stretched, dried, and heat treated. describes a technique for producing flame-resistant, high-strength, and high-modulus fibers. Also, Journal of the Japan Textile Society, 40, T-480<198
4+ and Japanese Unexamined Patent Publication No. 59-157319, etc., a spinning dope with improved wet coagulability is obtained by ring-closing a part of polyamic acid into polyimide, and a filament obtained by wet spinning the same. It is described that polyimide fibers with excellent mechanical properties can be obtained by immersing the fiber in an acetic anhydride/pyridine system to promote imidization, and then heat-treating the fiber after drying. However, the mechanical properties of fibers obtained by either method do not reach a level that is satisfactory as high-performance fibers. This is because -a is a polymer with a rigid skeleton and when high mechanical properties are obtained by solution molding, the molding dope has fluid birefringence, as typified by the manufacturing method of poly-p-phenylene terephthalamide. Furthermore, it is an important condition to exhibit optical anisotropy. This is because the polymer molecular chains form an aggregate structure called a domain, which creates a state in which they are highly oriented before molding, and as a result, it is possible to obtain a molded product in which orientation is highly promoted. be. In the case of rigid skeleton polyimide, the polyamic acid dope for molding has fluid birefringence,
Furthermore, not only does it not exhibit optical anisotropy, but even if the final polyimide is rigid, the polyamic acid that is the precursor for its molding is as follows (Ar is a rigid skeleton diamine residue). ) It has a skeleton in which a p-oriented body as in (1) and an m-oriented body as in (2) coexist, and therefore the polymer molecular chain is not straight but in a bent wire-like state. Therefore, it is difficult to promote orientation during molding, and the resulting mechanical properties do not exhibit satisfactory values. On the other hand, JP-A-60-65112
As shown in the above publications, a method has been proposed in which the polyimide skeleton is made somewhat flexible to obtain solvent-soluble polyimide, and this is molded to obtain high-strength fibers. Therefore, high modulus cannot be achieved.

(発明の目的) 本発明の主たる目的は、上述の如き、先行技術の問題点
を解決し、耐熱性及び力学的性質の優れたポリイミド成
形体、特に繊維、フィルムバルブ状粒子等を製造する際
に有用な新規な成形用ドープ、就中、ポリイミド成形用
ドープとしては従来にない流動複屈折性を示し、成形時
に高度に配向しやすい成形用ドープを提供することにあ
る。
(Objective of the Invention) The main object of the present invention is to solve the problems of the prior art as described above, and to produce polyimide molded articles with excellent heat resistance and mechanical properties, especially fibers, film bulb-shaped particles, etc. The object of the present invention is to provide a new molding dope useful for molding, especially a polyimide molding dope that exhibits unprecedented flow birefringence and is highly oriented during molding.

(発明の構成) すなわち、本発明は、主たる構成単位が下記(I)式よ
りなるポリイミドを硫酸及び/又はメタンスルホン酸に
溶解せしめてなるドープであって、該ドープは流動複屈
折性を示すことを特徴とする新規成形用ドープ である。
(Structure of the Invention) That is, the present invention provides a dope prepared by dissolving a polyimide whose main structural unit is represented by the following formula (I) in sulfuric acid and/or methanesulfonic acid, and the dope exhibits flow birefringence. This is a new molding dope characterized by the following.

本発明で用いられる上記(I>式で表わされる構成単位
からなるポリイミドは、ピロメリット酸もしくはその誘
導体と2.2′−ジメチルベンジジンもしくはその誘導
体とを反応させる方法により製造される。
The polyimide comprising the structural unit represented by the above formula (I>) used in the present invention is produced by a method of reacting pyromellitic acid or a derivative thereof with 2,2'-dimethylbenzidine or a derivative thereof.

例えば、無水ピロメリット酸と2,2′−ジメチルベン
ジジンを溶媒中で反応させてポリアミド酸を製造した後
、加熱するか又は無水酢酸等の化学的イミド化剤を用い
てイミド化する方法により容易に製造できる。しかし、
他の方法例えばピロメリット酸のジエステルジ塩化物を
用いる方法、あるいは2.2′−ジメチルベンジジンか
ら誘導されるジイソシアネートを用いる方法等により製
造されたものであっても本願の目的を達成できることは
いうまでもない。
For example, it is easy to produce polyamic acid by reacting pyromellitic anhydride and 2,2'-dimethylbenzidine in a solvent, and then imidizing it by heating or using a chemical imidizing agent such as acetic anhydride. can be manufactured. but,
It goes without saying that the object of the present application can be achieved even if the product is produced by other methods, such as a method using diester dichloride of pyromellitic acid or a method using a diisocyanate derived from 2,2'-dimethylbenzidine. Nor.

かかるポリイミドを製造する際の反応溶媒については、
上記の如き原料モノマーを溶解し、かつそれらと実質的
に非反応性であり、好ましくは固有粘度が少なくと61
,0以上、より好ましくは1゜2以上のポリマーを得る
ことが可能なものであれば如何なる溶媒も使用できる。
Regarding the reaction solvent when producing such polyimide,
It dissolves the raw material monomers as mentioned above, is substantially non-reactive with them, and preferably has an intrinsic viscosity of at least 61
, 0 or more, more preferably 1.degree.

例えば、N、N。For example, N, N.

N’、N’ −テトラメチル尿素(TMU) 、N、N
−ジメチルアセトアミド(DMAC) 、N、N−ジエ
チルアセトアミド(DEAC) 、N、N−ジメチルプ
ロピオンアミド<DMPR) 、N、N−ジメチルブチ
ルアミド(NMBA) 、N、N−ジメチルイソブチル
アミド(NMIB)、N−メチルピロリドン−2(NM
P) 、N−エチルピロリドン−2(NEP)、N−メ
チルカプロラクタム(NMC) 、N、N−ジメチルメ
トキシアセトアミド、N−アセチルピロリジン(NAP
R) 、N−アセチルビペリジン、N−メチルピペリド
ン−2(NMPD)、N、N’ −ジメチルエチレン尿
素、N、N’−ジメチルプロピレン尿素、N、N。
N',N'-tetramethylurea (TMU), N,N
-dimethylacetamide (DMAC), N,N-diethylacetamide (DEAC), N,N-dimethylpropionamide<DMPR), N,N-dimethylbutyramide (NMBA), N,N-dimethylisobutyramide (NMIB), N-methylpyrrolidone-2 (NM
P), N-ethylpyrrolidone-2 (NEP), N-methylcaprolactam (NMC), N,N-dimethylmethoxyacetamide, N-acetylpyrrolidine (NAP)
R), N-acetylbiperidine, N-methylpiperidone-2 (NMPD), N,N'-dimethylethyleneurea, N,N'-dimethylpropyleneurea, N,N.

N’、N’−テトラメチルマロンアミド、N−アセチル
ピロリドン等のアミド系溶媒、p−クロルフェノール、
フェノール、m−クレゾール、p−クレゾール、2.4
−ジクロルフェノール等のフェノール系溶媒もしくはこ
れらの混合物をあげることができる。ポリマーの製造は
、前記モノマーを脱水した上記の溶媒中で通常の溶液重
合法と同様に製造する。この際の反応温度は一般に80
℃以下、好ましくは60℃以下とする。温度が高すぎる
と加水分解反応が起こることがあるなめ好ましくない。
Amide solvents such as N', N'-tetramethylmalonamide and N-acetylpyrrolidone, p-chlorophenol,
Phenol, m-cresol, p-cresol, 2.4
- Phenolic solvents such as dichlorophenol or mixtures thereof can be mentioned. The polymer is produced in the same manner as the usual solution polymerization method in the above-mentioned solvent in which the monomer is dehydrated. The reaction temperature at this time is generally 80
℃ or lower, preferably 60℃ or lower. If the temperature is too high, a hydrolysis reaction may occur, which is not preferable.

また、この時の濃度はモノマー濃度として1〜20wt
%程度が好ましい。
Also, the concentration at this time is 1 to 20 wt as monomer concentration.
% is preferable.

かくして得られるポリマーは、一般的にはポリイミドの
前駆体であるポリアミド酸もしくはポリアミドエステル
等の場合が多い。本発明においては、かかるポリイミド
前駆体はさらに反応させ、ポリイミドとして使用する必
要がある。
The polymer thus obtained is generally polyamic acid or polyamide ester, which is a precursor of polyimide. In the present invention, such a polyimide precursor needs to be further reacted and used as a polyimide.

このイミドとする方法は、従来より公知の如何なる方法
を採用してもよいが、−a的な方法としては加熱による
方法と化学的に行なう方法があり、いずれも採用できる
。ここに加熱による方法とは前駆体を100℃以上、好
ましくは150℃以上に加熱してイミドとする方法であ
り、また化学的に行なう方法とは無水酢酸等の化学的脱
水剤によりイミドとする方法である。
Any conventionally known method may be used to form the imide, and the -a method includes a heating method and a chemical method, both of which can be employed. Here, the heating method refers to a method in which a precursor is heated to 100°C or higher, preferably 150°C or higher to form an imide, and the chemical method refers to a method in which a precursor is formed into an imide using a chemical dehydrating agent such as acetic anhydride. It's a method.

なお、かかるイミド化反応においては、あまりに長時間
加熱しすぎると得られるポリマーの溶媒への溶解性が悪
くなる傾向があり、加熱条件は適宜選択する必要がある
。もっとも不溶部分が存在していても、その量は掻く少
量で大部分は溶解可能であるため、不溶部分を分離、例
えば炉別することにより何等問題のない成形用ドープが
得られる。また、ポリイミド前駆体としてはポリアミド
エステルの方が、ポリアミド酸より溶解性のよいものが
得やすい傾向にあり好ましい。
In addition, in such an imidization reaction, heating conditions for too long tend to deteriorate the solubility of the resulting polymer in the solvent, so the heating conditions must be selected appropriately. Even if an insoluble portion is present, most of it can be dissolved in a small amount. Therefore, by separating the insoluble portion, for example, by separating it in a furnace, a molding dope without any problems can be obtained. Further, as the polyimide precursor, polyamide ester is preferable because it tends to be more soluble than polyamide acid.

また、ポリイミド前駆体は通常溶液の形で得られるので
、そのまま化学的方法もしくは加熱する方法でイミド化
する場合には、ポリイミドはスラリーの形態で得られる
In addition, since polyimide precursors are usually obtained in the form of a solution, if imidization is directly performed by a chemical method or a heating method, the polyimide is obtained in the form of a slurry.

かかる前駆体溶液又はポリイミド混合物より前駆体又は
ポリイミドを分離するには、水その他の貧溶媒と混合す
る等一般的によく知られている方法をそのまま採用すれ
ばよい。またこの分離操作とイミド化操作はいずれを先
に行ってもよい。かくして得られるポリイミドは通常粉
末状であるが、その他のどの様な形態であってもよい。
In order to separate the precursor or polyimide from such a precursor solution or polyimide mixture, a generally well-known method such as mixing with water or other poor solvent may be used as is. Further, either of the separation operation and the imidization operation may be performed first. The polyimide thus obtained is usually in powder form, but may be in any other form.

なお、次の溶解操作に用いる前に一旦乾燥して使用され
る。
Note that it is used after being dried before being used for the next dissolution operation.

本発明で使用されるポリイミドは上記の如く製造された
ものであるが、これらは通常1.0以上、好ましくは1
.5以上、さらに好ましくは2.0以上の固有粘度を有
することが好ましい。なおここでいう固有粘度は35℃
硫酸中で測定した値である。
The polyimide used in the present invention is produced as described above, and usually has a polyimide of 1.0 or more, preferably 1.
.. It is preferable to have an intrinsic viscosity of 5 or more, more preferably 2.0 or more. Note that the intrinsic viscosity here is 35°C.
This is a value measured in sulfuric acid.

本発明においてはかかるポリイミドを硫酸及び/又はメ
タンスルホン酸に溶解させて流動複屈折性を有する本発
明のドープを得る。
In the present invention, such a polyimide is dissolved in sulfuric acid and/or methanesulfonic acid to obtain the dope of the present invention having flow birefringence.

本発明で用いられる硫酸は濃度98%以上の硫酸であっ
て30%以下の発煙硫酸まで含むものである。
The sulfuric acid used in the present invention has a concentration of 98% or more and contains up to 30% fuming sulfuric acid.

特に溶解した溶液において、水分が殆んどない状態とす
ることが好ましい一つの方法である。また、メタンスル
ホン酸にあっても水分は出来るだけ少ない方が好ましい
。かかる硫酸とメタンスルホン酸は混合して用いてもよ
い。
In particular, one method that is preferable is to bring the dissolved solution into a state in which almost no water is present. Further, it is preferable that the amount of water in methanesulfonic acid is as low as possible. Such sulfuric acid and methanesulfonic acid may be used in combination.

本発明のドープは、前記の如きポリイミドを上記の如き
溶媒に溶解して得るのであるが、濃度は5重量%以上、
好ましくは8重量%以上として、該ドープが流動複屈折
性を示す濃度にする必要がある。なお、この濃度はポリ
イミドの分子量等によっても異なるので、必ずしも一義
的に定めることは出来ない。この流動複屈折性は、簡易
的には直交偏光板間に置いた二枚のガラス板の間にドー
プをはさみ、若干のすり変形を与えた時、暗視野から明
視野に変化することより確認できる。すり変形後静止下
で明視野となる場合も当然含まれる。
The dope of the present invention is obtained by dissolving the above-mentioned polyimide in the above-mentioned solvent, and the concentration is 5% by weight or more,
The concentration should preferably be 8% by weight or more, so that the dope exhibits flow birefringence. Note that since this concentration varies depending on the molecular weight of the polyimide, etc., it cannot necessarily be determined unambiguously. This flow birefringence can be confirmed simply by sandwiching the dope between two glass plates placed between orthogonal polarizing plates and observing the change from dark field to bright field when a slight abrasion deformation is applied. Naturally, this also includes the case where a bright field appears under static conditions after sliding deformation.

また、ピストン式で小孔よりドープを押出す方式の粘度
計でも確認でき、流動複屈折性を示す際には、ピストン
にかける荷重がある値を越すと荷重を増しても粘度が下
がらず、場合によっては高くなる現象が起る。
It can also be confirmed using a piston-type viscometer that extrudes the dope through a small hole, and when exhibiting flow birefringence, the viscosity does not decrease even if the load is increased if the load applied to the piston exceeds a certain value. In some cases, the phenomenon of becoming higher occurs.

以上詳述した本発明のドープは成形性に優れ、湿式法あ
るいはドライジェット湿式法により繊維、フィルムパル
プ状粒子等に成形することができる。
The dope of the present invention described in detail above has excellent moldability and can be molded into fibers, film pulp-like particles, etc. by a wet method or a dry jet wet method.

(発明の作用・効果) 本発明が対象とする剛直骨格ポリイミドの場合、−mに
は溶解すべき溶媒がなく、また例え溶解できたとしても
、流動複屈折性を示すが如き高濃度の溶液が得られるこ
とはこれまで想像もされなかった。しかるに、本発明で
用いるポリイミドからは、流動複屈折性を示すが如き高
濃度のドープが形成されうるのである。
(Operations and Effects of the Invention) In the case of the rigid skeleton polyimide targeted by the present invention, -m does not have a solvent to be dissolved, and even if it can be dissolved, the solution is so concentrated that it exhibits flow birefringence. It was never imagined that this could be achieved. However, from the polyimide used in the present invention, a highly concentrated dope exhibiting flow birefringence can be formed.

このドープは、成形時には高度な配向状態が形成され、
従って耐熱、及び力学的特性の優れたポリイミド成形体
を得ることが可能となる。特に本発明のドープから紡糸
した繊維は、耐熱性繊維として、また、高強度・高モジ
ュラス繊維として、ローブ、ベルト、絶縁布、r布、ハ
ニカム構造材料等の分野や、タイヤ等のゴム製品、熱硬
化性又は熱可塑性樹脂の補強材、更には防護衣料等の分
野に広く使用することができる。
This dope forms a highly oriented state during molding,
Therefore, it becomes possible to obtain a polyimide molded article with excellent heat resistance and mechanical properties. In particular, the fiber spun from the dope of the present invention can be used as a heat-resistant fiber and as a high-strength/high-modulus fiber in fields such as robes, belts, insulating cloth, R cloth, honeycomb structure materials, and rubber products such as tires. It can be widely used in the fields of thermosetting or thermoplastic resin reinforcing materials, as well as protective clothing.

(実施例) 以下本発明を実施例を挙げて説明する。なお実施例中固
有粘度(IV>は100%硫酸中35℃で測定したもの
である。
(Example) The present invention will be described below with reference to Examples. In the examples, the intrinsic viscosity (IV>) was measured in 100% sulfuric acid at 35°C.

実施例1 無水ピロメリット酸(PMDA)とメタノールとを混合
、反応させた後、メタノールを留出乾固したジメチルエ
ステルを塩化チオニル中で環流反応させた。得られた反
応物を冷却後沈殿物を濾別し、トルエンで再結晶して得
られる酸塩化物はNMR1赤外分析の結果、2.5−ジ
カルボメトキシテレフタル酸塩化物(A)であることを
確認した。
Example 1 Pyromellitic anhydride (PMDA) and methanol were mixed and reacted, and then the methanol was distilled to dryness and dimethyl ester was refluxed in thionyl chloride. After cooling the obtained reaction product, the precipitate was filtered, and the acid chloride obtained by recrystallizing with toluene was found to be 2,5-dicarbomethoxyterephthalic acid chloride (A) as a result of NMR1 infrared analysis. It was confirmed.

300℃で脱水乾燥した塩化カルシウムをN−メチルピ
ロリドン(NMP)に2 wtX溶解し、さらにモレキ
ュラーシブスで脱水した溶液を重合溶媒とし2,2′−
ジメチルベンジジン4.83gを上記溶媒150 ml
中に乾燥窒素気流中で溶解した。このアミン溶液を外部
冷却により一10℃に保ち上述の酸塩化物(A)を7.
31g添加し、重合反応せしめた。
2,2'-
Add 4.83 g of dimethylbenzidine to 150 ml of the above solvent.
The mixture was dissolved in a stream of dry nitrogen. This amine solution was kept at -10°C by external cooling and the above acid chloride (A) was added in 7.
31g was added to cause a polymerization reaction.

酸塩化物(A)が完全に溶解し、溶液が徐々に粘稠とな
ったところでピリジン5mlを添加し、かつ温度を50
℃に上昇させると反応は急速に進行し、溶液が粘稠とな
るとともに一部重合物の析出が見られた。さらに攪拌を
2時間続行し重合反応を終了した。反応終了後、常温に
戻し大量のメタノール中に投入し重合体を析出させた。
When the acid chloride (A) was completely dissolved and the solution gradually became viscous, 5 ml of pyridine was added and the temperature was lowered to 50 ml.
When the temperature was raised to 0.degree. C., the reaction proceeded rapidly, the solution became viscous, and some polymers were observed to precipitate. Stirring was further continued for 2 hours to complete the polymerization reaction. After the reaction was completed, the temperature was returned to room temperature and the mixture was poured into a large amount of methanol to precipitate a polymer.

得られた重合体をr別し、さらにメタノール、アセトン
で洗浄後、真空乾燥しな。
The obtained polymer is separated, further washed with methanol and acetone, and then vacuum dried.

このポリマーを200℃で1時間熱処理した。得られた
ポリマーは、赤外線吸収スペクトルの測定結果より、は
ぼ完全にイミドに転換しているものであった。このポリ
マーを濃硫酸と発煙硫酸を用いて調合した100%硫酸
に溶解して測定した固有粘度は1.80であった。
This polymer was heat treated at 200°C for 1 hour. The obtained polymer was almost completely converted to imide, as determined by the measurement results of infrared absorption spectrum. The intrinsic viscosity measured by dissolving this polymer in 100% sulfuric acid prepared using concentrated sulfuric acid and fuming sulfuric acid was 1.80.

上記ポリマーを100%硫酸中に各種の濃度で溶解した
ものの物性を表に示す。
The physical properties of the above polymer dissolved in 100% sulfuric acid at various concentrations are shown in the table.

なお表中、「流動複屈折性」とは得られた溶液を顕微鏡
によりクロスニコル下で観察し、若干のすり変形時に光
の透過が見られたかどうかで示し、粘度は高化式フロー
テスターにおいて孔径0.7mm、長さ10mmの孔よ
りドープを流出させた際の値を示す。
In the table, "flow birefringence" indicates whether the obtained solution was observed under crossed nicols using a microscope and light transmission was observed during slight abrasion deformation, and viscosity was determined by observing the obtained solution under crossed nicol conditions using a Koka type flow tester. The values are shown when dope is flowed out from a hole with a hole diameter of 0.7 mm and a length of 10 mm.

Claims (1)

【特許請求の範囲】[Claims] (1)主たる構成単位が下記( I )式よりなるポリイ
ミドを硫酸及び/又はメタンスルホン酸に溶解せしめて
なるドープであって、該ドープは流動複屈折性を示すこ
とを特徴とする新規成形用ドープ。 ▲数式、化学式、表等があります▼( I )
(1) A dope made by dissolving a polyimide whose main structural unit is represented by the following formula (I) in sulfuric acid and/or methanesulfonic acid, for new molding, characterized in that the dope exhibits flow birefringence. Dope. ▲There are mathematical formulas, chemical formulas, tables, etc.▼(I)
JP8810089A 1989-04-10 1989-04-10 Novel dope for shaping Pending JPH02269156A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8810089A JPH02269156A (en) 1989-04-10 1989-04-10 Novel dope for shaping

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8810089A JPH02269156A (en) 1989-04-10 1989-04-10 Novel dope for shaping

Publications (1)

Publication Number Publication Date
JPH02269156A true JPH02269156A (en) 1990-11-02

Family

ID=13933451

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8810089A Pending JPH02269156A (en) 1989-04-10 1989-04-10 Novel dope for shaping

Country Status (1)

Country Link
JP (1) JPH02269156A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006257125A (en) * 2005-03-15 2006-09-28 Teijin Ltd Optically anisotropic dope

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006257125A (en) * 2005-03-15 2006-09-28 Teijin Ltd Optically anisotropic dope

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