JPH0742611B2 - Polyimide fiber - Google Patents

Polyimide fiber

Info

Publication number
JPH0742611B2
JPH0742611B2 JP63087313A JP8731388A JPH0742611B2 JP H0742611 B2 JPH0742611 B2 JP H0742611B2 JP 63087313 A JP63087313 A JP 63087313A JP 8731388 A JP8731388 A JP 8731388A JP H0742611 B2 JPH0742611 B2 JP H0742611B2
Authority
JP
Japan
Prior art keywords
polyimide
fiber
yarn
solution
imidization
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
JP63087313A
Other languages
Japanese (ja)
Other versions
JPH01261421A (en
Inventor
克男 功刀
紀次 斎木
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 JP63087313A priority Critical patent/JPH0742611B2/en
Publication of JPH01261421A publication Critical patent/JPH01261421A/en
Publication of JPH0742611B2 publication Critical patent/JPH0742611B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)
  • Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)
  • Artificial Filaments (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

(産業上の利用分野) 本発明は宇宙・航空分野或いは電子材料分野等において
有用なポリイミドよりなる新規高弾性率繊維に関するも
のである。 (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
酸無水物より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。 一方、先端技術の高度化により宇宙・航空機用途、電子
材料用途等の分野において、より高い耐熱性と高強力・
高弾性率等の機械的性質を合わせ持つ繊維、フィルム等
が近年要求されるようになっている。そこで、耐熱性に
優れるポリイミドの機械的特性を向上せしめるために剛
直骨格ポリイミドの重要性が認識されつつある。 ところで、ポリイミドの一般的な製法としては、ポリイ
ミドは不溶・不融のものが多いことからその前駆体であ
るポリアミド酸と溶媒とからなる成形用ドープを環式ま
たは湿式成形し、その成形過程においてポリアミド酸を
閉環せしめ、ポリイミド成形体を得る方法が採用されて
いる。この場合、ポリ−p−フェニレン(或いは4,4′
−ビフェニレン)ピロメリットイミドの如き完全剛直骨
格を形成するものは、その剛直性ゆえにイミド化の過程
で結晶化が急速に進行するため熱延伸性に劣り、その結
果高度な機械的性質が発現されないという問題がある。
例えば、繊維学会誌Vo1.40,No.12、T−480〜T−487に
も記載されているように、ポリ−4,4′−ビフェニレン
ピロメリットイミドからは初期弾性率1,000g/de以上、
強度10g/de以上といった高弾性、高強度の繊維は得られ
ない。 上記の問題点を考慮して、分子鎖の剛直性を極度に低下
させることなく結晶性を低下せしめ成形性を向上させる
ことにより、良好な機械的性質を示すコポリイミドが種
々提案されているが(特開昭61-188127号公報、特開昭6
2-79227号公報)、これらは共重合体ゆえにそのポテン
シャル、即ち結晶弾性率のレベルダウンは否めず、まし
てや成形法の改良による物性の更なる向上も望めない。 (発明の目的) 本発明の目的は上述の問題点を解決し、共重合によるこ
となく、しかも結晶性を大幅に損なうことなく成形性の
改善されたポリイミドよりなる、極めて優れた機械的性
質を有する繊維を提供することにある。 (発明の構成) 本発明者らは、上記目的を達成せんとして鋭意研究した
結果、特定の化学構造を有するポリイミドのホモポリマ
ーは剛直骨格でありながらも成形性に優れていて高倍率
に延伸することができ、高度な機械的特性を有するポリ
イミド繊維が得られることを見い出し、本発明を完成す
るに至った。 かくして本発明によれば、下記(I)式で表わされる単
位を主たる繰返し単位とするポリイミドよりなる繊維で
あって、該繊維の初期弾性率が1,000g/de以上、且つ引
張強度が15g/de以上であるポリイミド繊維が提供され
る。 本発明におけるポリイミドは、ピロメリット酸ジ酸無水
物、もしくは3,3′,4,4′−ジフェニルテトラカルボン
酸ジ酸無水物又はその誘導体と2,2′−ジメチルベンジ
ジン及び/又はその塩酸塩とから有機溶媒中で合成され
る。ここで、“主たる”とは、ポリイミドの繰返し単位
の90%以上、好ましくは95%以上が上記(I)であるこ
とを意味し、他の構成成分がその範囲を逸脱して含まれ
るような場合には、結晶性の低下等の影響により本発明
の目的を達成することはできない。 本発明で用いられる上記芳香族ジ酸無水物の誘導体とし
ては、ジエステル、ジエステルジ酸クロライド等をあげ
ることができる。 なお、かかるジエステルジ酸クロリドは、芳香族ジ酸無
水物とアルコール、フェノール類とから合成されたテト
ラカルボン酸ジエステルをチオニルクロライド等を用い
る通常の酸クロライド化法で合成されるが、始めのエス
テル化においては反応性及び得られたポリマーの溶解性
等から脂肪族のアルコール、エーテル基を含有する脂肪
族のアルコールを使用するのが好ましい。 次に本発明にて用いられる有機溶媒としては次のような
ものが上げられる。
(Field of Industrial Application) The present invention relates to a novel high modulus fiber made of polyimide which is useful in the fields of space and aviation, electronic materials and the like. (Prior art) Conventionally, polyimide has heat resistance, mechanical properties, electrical properties,
It is known to be useful as a raw material for fibers, films and other molded articles having excellent weather resistance. For example, 4,
A film having excellent heat resistance is obtained from a polyimide produced from 4'-diaminodiphenyl ether and pyromellitic dianhydride, and is widely used for electrical insulation applications. On the other hand, due to the sophistication of advanced technology, it has higher heat resistance and higher strength in fields such as space and aircraft applications and electronic material applications.
In recent years, fibers, films and the like having mechanical properties such as high elastic modulus have been required. Therefore, the importance of rigid skeleton polyimide is being recognized in order to improve the mechanical properties of polyimide having excellent heat resistance. By the way, as a general manufacturing method of polyimide, since polyimide is often insoluble and infusible, a molding dope composed of a polyamic acid which is a precursor thereof and a solvent is cyclically or wet molded, and in the molding process thereof. A method of closing a polyamic acid to obtain a polyimide molded body has been adopted. In this case, poly-p-phenylene (or 4,4 '
-A biphenylene) pyromellitimide, which forms a completely rigid skeleton, is inferior in heat stretchability because crystallization rapidly progresses in the process of imidization due to its rigidity, and as a result, high mechanical properties are not expressed. There is a problem.
For example, as described in Textile Society of Japan, Vo1.40, No. 12, T-480 to T-487, poly-4,4'-biphenylenepyromellitimide has an initial elastic modulus of 1,000 g / de or more. ,
Fibers with high elasticity and strength of 10 g / de or more cannot be obtained. In consideration of the above problems, by improving the moldability by lowering the crystallinity without significantly reducing the rigidity of the molecular chain, various copolyimides showing good mechanical properties have been proposed. (JP-A 61-188127, JP-A 6-188127
No. 2-79227), since these are copolymers, their potential, that is, the level of crystal elastic modulus, cannot be denied, and further improvement of physical properties due to improvement of molding method cannot be expected. (Object of the invention) An object of the present invention is to solve the above-mentioned problems and to form a polyimide having improved moldability without copolymerization, and without significantly impairing crystallinity, and having extremely excellent mechanical properties. To provide a fiber having. (Structure of the Invention) As a result of intensive studies conducted by the present inventors in order to achieve the above object, a homopolymer of a polyimide having a specific chemical structure has a rigid skeleton but is excellent in moldability and can be stretched at a high ratio. It was found that a polyimide fiber having a high mechanical property can be obtained, and the present invention has been completed. Thus, according to the present invention, there is provided a fiber composed of a polyimide having a unit represented by the following formula (I) as a main repeating unit, the fiber having an initial elastic modulus of 1,000 g / de or more and a tensile strength of 15 g / de. A polyimide fiber as described above is provided. The polyimide in the present invention is pyromellitic dianhydride, or 3,3 ′, 4,4′-diphenyltetracarboxylic acid dianhydride or its derivative and 2,2′-dimethylbenzidine and / or its hydrochloride. It is synthesized from and in an organic solvent. Here, "mainly" means that 90% or more, preferably 95% or more, of the repeating unit of the polyimide is the above (I), and other constituent components are included outside the range. In this case, the object of the present invention cannot be achieved due to the influence of deterioration of crystallinity. Examples of the derivative of the aromatic diacid anhydride used in the present invention include diester and diester diacid chloride. Incidentally, such diester diacid chloride is a tetracarboxylic acid diester synthesized from an aromatic diacid anhydride, an alcohol, and a phenol, which is synthesized by a usual acid chloride method using thionyl chloride or the like. In the above, it is preferable to use an aliphatic alcohol or an ether group-containing aliphatic alcohol in view of reactivity and solubility of the obtained polymer. Next, the following organic solvents are used in the present invention.

【有機溶媒】[Organic solvent]

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
(NMP)、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(NAPR)、N−アセ
チルピペリジン、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′−テトラメチルマロンアミド、
N−アセチルピロリドン、シメチルスルホキシド(DMS
O)、ヘキサメチルホスホルアミド(HMPA)。 また、芳香族ジ酸無水物として3,3′,4,4′−ジフェニ
ルテトラカルボン酸ジ酸無水物を用いる際には、フェノ
ール系の溶媒を使用することも可能である。 上記のモノマーを上記溶媒中で溶液重合することにより
本発明しのポリイミドの前駆体が合成される。
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
(NMP), N-ethylpyrrolidone-2 (NEP), N-methylcaprolactam (NMC), N, N-dimethylmethoxyacetamide, N-acetylpyrrolidine (NAPR), N-acetylpiperidine, N-methylpiperidone-2 (NMPD) ),
N, N'-dimethylethyleneurea, N, N'-dimethylpropyleneurea, N, N, N ', N'-tetramethylmalonamide,
N-acetylpyrrolidone, dimethyl sulfoxide (DMS
O), hexamethylphosphoramide (HMPA). When 3,3 ', 4,4'-diphenyltetracarboxylic acid diacid anhydride is used as the aromatic diacid anhydride, a phenolic solvent can be used. The polyimide precursor of the present invention is synthesized by solution polymerization of the above monomers in the above solvent.

【ポリイミド前駆体の合成】[Synthesis of polyimide precursor]

ポリイミド前駆体の合成法としては、芳香族ジアミンと
芳香族テトラカルボン酸無水物及び/又はその誘導体と
から主としてなるモノマーを組合わせて溶液重合する方
法が採用される。 後掲の実施例1に示すように、2,2′−ジメチルベンジ
ジンを溶解したNMP溶液を−10℃に保ちながら、ピロメ
リット酸ジ無水物を上記ジアミンのほぼ当量添加し激し
く攪拌すると溶液は次第に粘度を増し、更に攪拌を続け
ると高粘度の溶液が得られ、固有粘度を測定したところ
5.2であり、高重合度のポリアミド酸が生成されている
ことが確認された。固有粘度(ηinh)の測定はNMP中35
℃、濃度0.5g/dlでオストワルド粘度計を用いて1/C[ln
(t/t0)]により算出した。 またテトラカルボン酸ジエステルジ酸クロリド、或いは
2,2′−ジメチルベンジジンの塩酸塩を用いる場合も同
様に溶液重合を実施すればよいが、その際3級アミン等
の脱塩化水素剤を加えておくことも可能である。なお、
本発明のポリイミドを構成する2,2′−ジメチルベンジ
ンは剛直ジアミンの核置換誘導体であるが、塩素置換の
ものと比較して反応性に優れ高重合度のポリマーを得る
ことができる。また、価格的にも有利である。 以上の如くして芳香族ジ酸無水物及び/又はその誘導体
と2,2′−ジメチルベンジン及び/又はその塩酸塩とか
ら得られたポリイミド前駆体をイミド化することにより
本発明のポリイミドが合成される。イミド化は、後述の
化学環化剤の使用、或いは加熱により行われどちらを選
択してもよい。また本発明の目的を逸脱しない程度に共
重合成分を導入することは差し支えないが、その範囲は
ポリイミド1molに対し高々0.1mol程度である。 本発明のポリイミドはポリイミド本来の耐熱性に加え、
成形体として良好な機械的特性を示すが、これに関連し
て該ポリイミドよりなる繊維及びその製造法について詳
細に説明する。 本発明の繊維は、前述のポリイミド前駆体を含有する溶
液を、通常の乾式又は湿式成形し、得られた糸条をイミ
ド化することにより製造されるが、ポリイミド前駆体溶
液は次のように調整される。
As a method for synthesizing the polyimide precursor, a method in which a monomer mainly composed of an aromatic diamine and an aromatic tetracarboxylic acid anhydride and / or a derivative thereof is combined and solution-polymerized is adopted. As shown in Example 1 below, while maintaining the NMP solution in which 2,2′-dimethylbenzidine was dissolved at −10 ° C., pyromellitic dianhydride was added in an approximately equivalent amount of the above diamine and vigorously stirred to form a solution. When the viscosity was gradually increased and agitation was continued, a highly viscous solution was obtained, and the intrinsic viscosity was measured.
It was 5.2, and it was confirmed that a polyamic acid with a high degree of polymerization was produced. Intrinsic viscosity (ηinh) is measured in NMP 35
1 / C [ln at a temperature of 0.5g / dl with an Ostwald viscometer
(T / t 0 )]. In addition, tetracarboxylic acid diester diacid chloride, or
When 2,2'-dimethylbenzidine hydrochloride is used as well, solution polymerization may be carried out in the same manner, but it is also possible to add a dehydrochlorinating agent such as a tertiary amine at that time. In addition,
The 2,2'-dimethylbenzine constituting the polyimide of the present invention is a nucleus-substituted derivative of rigid diamine, but it is superior in reactivity as compared with the chlorine-substituted derivative and a polymer having a high degree of polymerization can be obtained. It is also advantageous in terms of price. As described above, the polyimide of the present invention is synthesized by imidizing the polyimide precursor obtained from the aromatic diacid anhydride and / or its derivative and 2,2′-dimethylbenzine and / or its hydrochloride. To be done. The imidization may be carried out by using a chemical cyclizing agent described later or by heating, and either one may be selected. Further, the copolymerization component may be introduced to the extent that it does not deviate from the object of the present invention, but the range is at most about 0.1 mol per 1 mol of polyimide. Polyimide of the present invention, in addition to the heat resistance of the original polyimide,
The molded article has good mechanical properties, and in this connection, the fiber made of the polyimide and the method for producing the fiber will be described in detail. The fiber of the present invention is produced by subjecting the solution containing the above-mentioned polyimide precursor to ordinary dry or wet molding, and imidizing the obtained yarn. The polyimide precursor solution is as follows. Adjusted.

【ポリイミド前駆体溶液の調整】[Preparation of polyimide precursor solution]

ポリイミド前駆体溶液の調整は、溶液重合を行ったポリ
イミド前駆体含有溶液を成形に適した粘度となるように
ポリマー濃度を調節し、該溶液をそのまま成形用ドープ
としてもよいし、また非溶液との混合等によりポリマー
を一旦単離後適当な溶媒に再溶解し、それを成形用ドー
プとすることもできる。 本発明では何れの方法も採用できるが、工業的には前者
の方法が好ましい。 糸条体への成形は、上記ポリイミド前駆体溶液を通常の
乾式又は湿式紡糸により実施される。該糸条は引き続き
イミド化されポリイミド繊維とされる。この繊維は初期
弾性率1,000g/de以上、引っ張り強度15g/de以上の優れ
た機械的特性を示し、先進複合材(A.C.M.)等の分野で
利用価値の高いものとして期待される。 さて、上記ポリイミドの潜在性能を発現せしめる本発明
の繊維製造法について詳細に説明する。
The polyimide precursor solution is adjusted by adjusting the polymer concentration so that the solution containing the polyimide precursor-containing solution has a viscosity suitable for molding, and the solution may be used as it is as a molding dope or as a non-solution. Alternatively, the polymer may be once isolated by, for example, mixing and re-dissolving in a suitable solvent to form a dope for molding. Although any method can be adopted in the present invention, the former method is industrially preferable. Molding into a filament is carried out by usual dry or wet spinning of the polyimide precursor solution. The yarn is subsequently imidized into a polyimide fiber. This fiber exhibits excellent mechanical properties with an initial elastic modulus of 1,000 g / de or more and a tensile strength of 15 g / de or more, and is expected to be highly useful in fields such as advanced composite materials (ACM). Now, the fiber production method of the present invention that brings out the latent performance of the polyimide will be described in detail.

【繊維製造法】[Fiber production method]

上述の如く調整されたポリイミド前駆体溶液を紡糸ノズ
ルより押し出し環式又は湿式成形法を用いて糸条への成
形及び脱溶媒を進行させる。この際、上記前駆体の溶媒
として高沸点のものを使用する場合が多いことから、湿
式の成形法を採用する方が好ましい。また、脱溶媒を進
行させる凝固剤としては、前駆体溶液の調整に用いた溶
媒と水との組み合せ、またはメタノール等の脂肪族のア
ルコールと水及び/又は前記溶媒との組み合せ等が用い
られるが、取扱い及びプロセスの簡便さからいって溶媒
と水との組み合せが好ましい。なお、糸条の凝固状態を
よりち密にするために適当な無機化合物を系内に含有さ
せてもなんら差し支えなく、また同様の目的で前駆体溶
液中に後述する化学環化材を添加し、前駆体の一部をイ
ミド化させておいてもよい。 以上の如く脱溶媒を進行せしめた糸条体は、そのまま、
或いはイミド化ののち熱延伸に供される。熱延伸時に高
張力を付与し分子配合を高度に促進させるためには熱延
伸前の糸条の強度を高めておくことが有効であり、その
ためには後者のイミド化のちの熱延伸が好ましい。 イミド化の手法は加熱によりポリアミド酸を脱水閉環さ
せる加熱イミド化法と2通りあるが、熱延伸前の結晶化
を抑制するためには後者が好ましい。以下、化学イミド
化法につい詳しく説明する。
The polyimide precursor solution prepared as described above is extruded from the spinning nozzle and the molding or desolvation of the yarn is promoted by a ring or wet molding method. At this time, since a solvent having a high boiling point is often used as the solvent for the precursor, it is preferable to adopt a wet molding method. As the coagulant for promoting desolvation, a combination of a solvent and water used for preparing a precursor solution, or a combination of an aliphatic alcohol such as methanol and water and / or the solvent may be used. A combination of a solvent and water is preferable in terms of handling and process convenience. Incidentally, there is no problem in containing an appropriate inorganic compound in the system in order to make the solidified state of the yarn denser, and for the same purpose, the chemical cyclization agent described below is added to the precursor solution, A part of the precursor may be imidized. As described above, the filamentous body that has undergone desolvation proceeds as it is,
Alternatively, it is subjected to thermal stretching after imidization. It is effective to increase the strength of the yarn before the hot drawing in order to give high tension during the hot drawing and to promote the molecular blending to a high degree. For that purpose, the latter hot drawing after imidization is preferable. There are two types of imidization methods, a heating imidization method in which a polyamic acid is dehydrated and ring-closed by heating, but the latter is preferable in order to suppress crystallization before hot drawing. Hereinafter, the chemical imidization method will be described in detail.

【化学イミド化法】 これは、無水酢酸等の脱水剤によりポリアミド酸の閉環
イミド化を進行せしめることを言い、この際触媒として
ピリジン等の3級アミンを併用してイミド化速度を大き
くすることもできる。糸条のイミド化においては、具体
的には凝固後の糸条をボビンに巻取った後、ボビンごと
上記の化学環化剤中に浸漬、或いは凝固後の糸条を化学
環化剤を配した浴中を通過させる等の手法により糸条と
化学環化剤とを接触せしめればよく、その手法に関して
は特に限定されるものではない。またこの際に、本発明
者らが先に特願昭62-272342号(特開平1-113434号)で
提案した糸条のイミド化促進手法を用いることにより、
より効果的にイミド化を進行せしめる事ができる。 上記のようにして得られた糸条は熱延伸工程に供されて
高度とな機械的特性を付与されるが、その際2倍以上に
引き延ばされることが不可欠であり、それ以下の延伸倍
率では本発明の高強度、高弾性率繊維を得ることはでき
ない。これは、一般にポリイミド繊維の成形においては
アラミド繊維の場合のような液晶紡糸が適用できないた
め、何等かの別の手法により高度な分子配合を達成せね
ばならないことによる。ここで、延伸温度は幅広く設定
することが可能であるが、溶媒の沸点−100℃以上、溶
媒の沸点+100℃以下で行うことが好ましく、これは前
者より低い温度での延伸は溶媒が系内に残存するため分
子鎖の緩和が大きく、効率的な延伸が困難であること、
また後者より高い温度での延伸は溶媒の急激な蒸発を伴
うため、ボイドの発生等優れた機械的特性の発現を妨げ
る欠陥部を生じさせる一因となるからである。しかしな
がら、段階的に昇温し延伸を進める場合はこの限りでは
ない。なお、延伸後、結晶化の促進とイミド化の完結及
び溶媒の除去のため高温での熱処理を採用することが好
ましく、の場合450℃以上650℃以下、より好ましくは50
0℃以上600℃以下の温度が採用される。 このようにして、本発明の弾性率1,000g/de以上、引張
り強度15g/de以上の優れた機械的特性を有する繊維が提
供される。 (発明の作用・効果) 本発明におけるポリイミドの最大の特徴は、剛直骨格で
あるにもかかわらず、かつ共重合成分を用いないにもか
かわらず、高倍率延伸が可能なことであり、高度な機械
的特性を有するポリイミド繊維を得ることが可能とな
る。なお、英国特許第903,271号公報には、ポリイミド
の構成成分として3,3′−ジメチルベンジジン、3,3′−
ジメトキシベンジジン等のベンジジン誘導体が記載され
ているが、これらを用いた剛直ポリイミドは、本発明の
ポリイミドに比較して熱延伸性に劣り、従って得られる
繊維の機械的特性も本発明のポリイミドには及ばない。 本発明の繊維は先進複合材料(A.C.M.)、電子材料等の
分野にて優れて性能を発揮するものである。 (実施例) 以下、本発明を実施例を挙げて説明する。例中の固有粘
度は(ηinh)はポリマー濃度0.5g/dlとなるよう前駆体
溶液を溶媒で稀釈して35℃にて測定、また引張特性は東
洋測器(株)製テンシロンを用い、試長100mm、引張速
度50mm/minで単糸について測定した。 実施例1
[Chemical imidization method] This means to promote ring-closure imidization of polyamic acid with a dehydrating agent such as acetic anhydride, in which case a tertiary amine such as pyridine is used as a catalyst to increase the imidization rate. You can also In the imidization of the yarn, specifically, after winding the coagulated yarn on a bobbin, the bobbin is immersed in the above-mentioned chemical cyclizing agent, or the coagulated yarn is placed on the chemical cyclizing agent. The yarn and the chemical cyclizing agent may be brought into contact with each other by a method such as passing through a bath, and the method is not particularly limited. Further, at this time, by using the yarn imidization promoting method previously proposed by the present inventors in Japanese Patent Application No. 62-272342 (JP-A-1-113434),
The imidization can be progressed more effectively. The yarn obtained as described above is subjected to a hot drawing process and imparted with high mechanical properties, but it is essential that the yarn is stretched to 2 times or more. Therefore, the high-strength, high-modulus fiber of the present invention cannot be obtained. This is because liquid crystal spinning, which is the case with aramid fibers, cannot generally be applied to the molding of polyimide fibers, and therefore a high degree of molecular blending must be achieved by some other method. Here, the stretching temperature can be set broadly, but it is preferable to carry out at a boiling point of the solvent of −100 ° C. or higher and a boiling point of the solvent of + 100 ° C. or lower. Since the remaining molecular weight is large, the relaxation of the molecular chain is large, and efficient stretching is difficult,
Further, stretching at a temperature higher than the latter is accompanied by rapid evaporation of the solvent, which is one of the causes for producing a defective portion that prevents the development of excellent mechanical properties such as generation of voids. However, this is not the case when the temperature is raised stepwise and the stretching is advanced. After stretching, it is preferable to employ a high temperature heat treatment for accelerating crystallization, completion of imidization and removal of the solvent, and in the case of 450 ° C. or higher and 650 ° C. or lower, more preferably 50
Temperatures above 0 ° C and below 600 ° C are used. Thus, the fiber of the present invention having excellent mechanical properties such as an elastic modulus of 1,000 g / de or more and a tensile strength of 15 g / de or more is provided. (Operation / Effect of Invention) The greatest feature of the polyimide in the present invention is that it can be stretched at a high ratio even though it has a rigid skeleton and does not use a copolymerization component. It becomes possible to obtain a polyimide fiber having mechanical properties. Incidentally, British Patent No. 903,271 discloses that 3,3'-dimethylbenzidine, 3,3'-, as a component of polyimide.
Although benzidine derivatives such as dimethoxybenzidine have been described, the rigid polyimides using these are inferior in the heat drawability as compared with the polyimide of the present invention, and therefore the mechanical properties of the obtained fiber are also in the polyimide of the present invention. It does not reach. The fiber of the present invention exhibits excellent performance in the fields of advanced composite materials (ACM), electronic materials and the like. (Examples) Hereinafter, the present invention will be described with reference to Examples. Intrinsic viscosity (ηinh) in the examples was measured at 35 ° C by diluting the precursor solution with a solvent so that the polymer concentration was 0.5 g / dl. Tensileon manufactured by Toyo Sokki Co., Ltd. was used for tensile properties. A single yarn was measured at a length of 100 mm and a pulling speed of 50 mm / min. Example 1

【ポリイミド前駆体の合成】[Synthesis of polyimide precursor]

脱水したNMP100mlに2,2′−ジメチルベンジジン5.59g
(26.3mmol)を溶解後、溶液を−10℃に冷却し、激しく
攪拌しつつピロメリット酸ジ酸無水物(PMDA)5.74g(2
6.3mmol)を添加した。引き続き重合を続け、溶液の粘
度上昇とともに順次NMPを追加し、最終的にポリマー濃
度4.5wt%の高粘度溶液を得た(I)。この間に要した
重合時間は約3時間であり、固有粘度は5.2に達した。
同様にして酸成分を変更して、3,3′,4,4′−ビフェニ
ルテトラカルボン酸ジ酸無水物(BPDA)と2,2′−ジメ
チルベンジシンとからなるポリマーを含む前駆体溶液
(II)を得た。 次に、ジアミン成分を2,2′−ジメチルベンジジンの塩
酸塩に変更し上記PMDAとの重合を行った。この際、脱塩
化水素剤としてピリジンをジアミンの2倍のモル数だけ
予め添加しておいたところ、(I)と同様の高粘度溶液
から得られた(III)。なお、これらの固有粘度は表−
1に示した。
5,2 g of 2,2'-dimethylbenzidine in 100 ml of dehydrated NMP
After dissolving (26.3 mmol), the solution was cooled to -10 ° C, and 5.74 g (2 mg of pyromellitic dianhydride (PMDA) was stirred vigorously.
6.3 mmol) was added. Polymerization was continued, NMP was added in sequence as the viscosity of the solution increased, and finally a high-viscosity solution having a polymer concentration of 4.5 wt% was obtained (I). The polymerization time required during this period was about 3 hours, and the intrinsic viscosity reached 5.2.
Similarly, by changing the acid component, a precursor solution containing a polymer composed of 3,3 ′, 4,4′-biphenyltetracarboxylic acid dianhydride (BPDA) and 2,2′-dimethylbenzidine ( II) was obtained. Next, the diamine component was changed to the hydrochloride of 2,2'-dimethylbenzidine and the polymerization with PMDA was performed. At this time, pyridine as a dehydrochlorinating agent was added in advance in an amount of twice the number of moles of diamine, and a high-viscosity solution similar to (I) was obtained (III). In addition, these intrinsic viscosities are
Shown in 1.

【湿式紡糸】[Wet spinning]

上述で得られた前駆体溶液をそのまま紡糸用ドープとし
て用い、減圧脱泡後、孔径0.3mm、孔数12のノズルを通
して水95/NMP5(容積比)からなる室温の凝固浴中に、
吐出速度5m/minで湿式紡糸し、凝固浴中を3m通過させた
のち室温の水よりなる延伸浴中にて延伸、脱溶媒を行っ
た。更に、得られた糸条を下記の2通りの方法で熱延伸
を行った。 (A法)得られた糸条を、連続して乾燥ドラムにて乾燥
し、更に150℃から550℃まで段階昇温して熱延伸を行っ
た。 (B法)得られた糸条を、一旦ガラス製のボビンに10分
間巻き取り、ボビンごと無水酢酸/ピリジン(容積比70
/30)からなる化学環化浴中に1時間浸漬しイミド化を
進行せしめ、該糸条を水洗・乾燥後、250℃にて熱延伸
し、更に550℃にて緊張下で処理した。 上記の紡糸時におけるドラフト、延伸倍率、熱延伸倍
率、及び得られたポリイミド繊維の単糸の引っ張り特性
を表−Iに示した。 比較例1 ジアミン成分、酸成分を種々変更し実施例1と同様に重
合し、次いで上記と同じく湿式紡糸し、得られた糸条を
(B法)により熱延伸した結果を表−IIに示した。ジア
ミン成分に3,3′−ジメチルベンジジン、3,3′−ジメト
キシベンジジンを用いたポリイミドは、実施例1の2,
2′−ジメチルベンジジンを用いたポリイミドに比較し
て熱延伸性に劣り、繊維物性についても同様であった。 比較例2 ジアミン成分、酸成分を種々変更したコポリイミドを実
施例1と同様に重合、湿式紡糸し、更に(B法)により
熱延伸した結果を表−IIIに示した。ホモポリマーに比
較して弾性率が低下していた。 実施例2 実施例1にて得られたPMDA及び2,2′−ジメチルベンジ
ジンを重合せしめた前駆体溶液(I)を湿式紡糸した糸
条を(B法)にて熱延伸する際に、種々延伸倍率を変更
した結果を表−IVに示した。2倍以上の熱延伸倍率によ
り、強度15g/de、弾性率1,000g/deが達成された。 実施例3 実施例1のPMDA及び2,2′−ジメチルベンジジンを重合
せしめた溶液(I)を湿式紡糸し、巻き取った糸条をボ
ビンごとメタノールを配した浴中に10分間浸漬し膨潤処
理したのち、(B法)に従って化学環化、及び熱延伸を
実施した。膨潤処理によりイミド化が促進され良好な繊
維物性が得られた。その結果を下記に示す。 熱延伸倍率:2.4 繊維物性(D/T/E/M):2.3/20.5/1.8/1,330 実施例4 実施例3の前駆体溶液(I)に無水酢酸をポリアミド酸
単位に対し0.4当量、ピリジンを無水酢酸と等モル添加
混合し、一夜放置し部分的にイミド化を進行せしめ、こ
れを紡糸用ドープ(IV)として用いた。以下、実施例3
の如く湿式紡糸、膨潤処理を施し、(B法)にて熱延伸
した。その結果を下記に示す。ドープの凝固性が改善さ
れ、繊維物性も更に向上していた。 熱延伸倍率:2.7 繊維物性(D/T/E/M):2.2/20.8/1.8/1,380
Using the precursor solution obtained above as a spinning dope as it is, after degassing under reduced pressure, in a coagulation bath at room temperature consisting of water 95 / NMP5 (volume ratio) through a nozzle having a pore diameter of 0.3 mm and a pore number of 12,
Wet spinning was performed at a discharge rate of 5 m / min, 3 m was passed through the coagulation bath, and then stretching and desolvation were performed in a stretching bath composed of water at room temperature. Further, the obtained yarn was hot-drawn by the following two methods. (Method A) The obtained yarn was continuously dried on a drying drum, and further heated stepwise from 150 ° C to 550 ° C to perform hot drawing. (Method B) The obtained yarn was once wound on a glass bobbin for 10 minutes, and acetic anhydride / pyridine (volume ratio 70
/ 30) was immersed in a chemical cyclization bath for 1 hour to promote imidization, the yarn was washed with water, dried, hot-drawn at 250 ° C, and further treated at 550 ° C under tension. The draft, the draw ratio, the hot draw ratio, and the tensile properties of the obtained polyimide fiber single yarn during spinning are shown in Table-I. Comparative Example 1 Polymerization was carried out in the same manner as in Example 1 except that the diamine component and the acid component were variously changed, and then wet spinning was performed as described above, and the obtained yarn was hot-stretched by the (method B). The results are shown in Table-II. It was The polyimide using 3,3′-dimethylbenzidine and 3,3′-dimethoxybenzidine as the diamine component is the same as in Example 1, 2.
The heat drawability was inferior to the polyimide using 2'-dimethylbenzidine, and the fiber properties were also the same. Comparative Example 2 Copolyimides having various diamine components and acid components were polymerized, wet-spun in the same manner as in Example 1, and further heat-stretched by (Method B). The results are shown in Table-III. The elastic modulus was lower than that of the homopolymer. Example 2 When the wet spinning of the precursor solution (I) obtained by polymerizing PMDA and 2,2′-dimethylbenzidine obtained in Example 1 was hot-stretched by (method B), The results of changing the draw ratio are shown in Table IV. A strength of 15 g / de and an elastic modulus of 1,000 g / de were achieved by a heat draw ratio of 2 times or more. Example 3 The solution (I) obtained by polymerizing PMDA and 2,2′-dimethylbenzidine of Example 1 was wet-spun, and the wound yarn was dipped in a bath containing methanol with bobbins for 10 minutes for swelling treatment. After that, chemical cyclization and hot stretching were performed according to (Method B). The swelling treatment promoted imidization and obtained good fiber properties. The results are shown below. Thermal draw ratio: 2.4 Fiber physical properties (D / T / E / M): 2.3 / 20.5 / 1.8 / 1,330 Example 4 Acetic anhydride was added to the precursor solution (I) of Example 3 in an amount of 0.4 equivalent based on the polyamic acid unit, and pyridine. Was mixed with acetic anhydride in an equimolar amount and allowed to stand overnight to partially promote imidization, which was used as a dope (IV) for spinning. Hereinafter, Example 3
As described above, wet spinning and swelling treatment were performed, and hot stretching was performed by (method B). The results are shown below. The coagulability of the dope was improved and the physical properties of the fiber were further improved. Thermal draw ratio: 2.7 Fiber physical properties (D / T / E / M): 2.2 / 20.8 / 1.8 / 1,380

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】下記(I)式で表わされる単位を主たる繰
返し単位とするポリイミドよりなる繊維であって、該繊
維の初期弾性率が1000g/de以上、且つ引張強度が15g/de
以上であるポリイミド繊維。
1. A fiber comprising a polyimide whose main repeating unit is a unit represented by the following formula (I), wherein the fiber has an initial elastic modulus of 1000 g / de or more and a tensile strength of 15 g / de.
The above is a polyimide fiber.
JP63087313A 1988-04-11 1988-04-11 Polyimide fiber Expired - Lifetime JPH0742611B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63087313A JPH0742611B2 (en) 1988-04-11 1988-04-11 Polyimide fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63087313A JPH0742611B2 (en) 1988-04-11 1988-04-11 Polyimide fiber

Publications (2)

Publication Number Publication Date
JPH01261421A JPH01261421A (en) 1989-10-18
JPH0742611B2 true JPH0742611B2 (en) 1995-05-10

Family

ID=13911352

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63087313A Expired - Lifetime JPH0742611B2 (en) 1988-04-11 1988-04-11 Polyimide fiber

Country Status (1)

Country Link
JP (1) JPH0742611B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5420232A (en) * 1992-04-29 1995-05-30 International Business Machines Corporation Process for making polyamic esters
TWI300744B (en) 2001-04-19 2008-09-11 Nippon Steel Chemical Co

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6025031A (en) * 1983-07-21 1985-02-07 Matsushita Electric Ind Co Ltd Manufacture of magnetic recording medium
JPS60250031A (en) * 1984-05-28 1985-12-10 Hitachi Ltd Low-thermal expansion resin material
JPS6279227A (en) * 1985-10-02 1987-04-11 Agency Of Ind Science & Technol Wholly aromatic copolypyromellitic imide
JPS6277921A (en) * 1985-10-02 1987-04-10 Agency Of Ind Science & Technol Fully aromatic copolyimide monoaxially oriented article

Also Published As

Publication number Publication date
JPH01261421A (en) 1989-10-18

Similar Documents

Publication Publication Date Title
CN102345177B (en) High-strength high-modulus polyimide fiber and preparation method thereof
KR0161313B1 (en) Polyimide amicester and process for preparing the same
CN102242415B (en) Method for improving spinnability and after processing characteristic of polyimide fiber
WO1991004300A1 (en) Miscible blends of polybenzimidazoles and polyamide-imides having fluorine-containing linking groups
JPS5910894B2 (en) Polyamide Hakumaku Knob Tree Textile Shitsuno
CA1329299C (en) Thermoplastically processible aromatic polyetheramide, process for its production and its use for the production of moldings
JP2517628B2 (en) New molding dope
JPH0140125B2 (en)
JPH0447048B2 (en)
JPH01260015A (en) Production of high-elastic modulus fiber
JPH01261421A (en) New polyimide, fiber comprising said polyimide and preparation thereof
JP2535405B2 (en) Copolyamic acid
JPH0455613B2 (en)
JPH0418115A (en) Production of polyimide fiber
JPS636028A (en) Preparation of polyimide molding
JP2728495B2 (en) Manufacturing method of copolyimide fiber
JP2695233B2 (en) Manufacturing method of copolyimide fiber
JPS6237051B2 (en)
JP2744464B2 (en) Method for producing copolyamic acid and copolyimide fiber
JPH036174B2 (en)
JPS6329008B2 (en)
JPH02269738A (en) Production of copolyamideamic acid and copolyamideimide fiber
JPS63230738A (en) Uniaxially oriented polyester-imide molding
JPH01113434A (en) Preparation of molded item of polyimide precursor
JPH0134534B2 (en)