JPS6097834A - Monoaxially orientated total aromatic copolyimide molded material - Google Patents

Monoaxially orientated total aromatic copolyimide molded material

Info

Publication number
JPS6097834A
JPS6097834A JP58205779A JP20577983A JPS6097834A JP S6097834 A JPS6097834 A JP S6097834A JP 58205779 A JP58205779 A JP 58205779A JP 20577983 A JP20577983 A JP 20577983A JP S6097834 A JPS6097834 A JP S6097834A
Authority
JP
Japan
Prior art keywords
solution
aromatic
molded material
orientated
strength
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
Application number
JP58205779A
Other languages
Japanese (ja)
Other versions
JPH036174B2 (en
Inventor
Takuma Kanda
神田 拓馬
Toshikazu Matsuda
敏和 松田
Masanori Sakamoto
正典 坂本
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP58205779A priority Critical patent/JPS6097834A/en
Publication of JPS6097834A publication Critical patent/JPS6097834A/en
Publication of JPH036174B2 publication Critical patent/JPH036174B2/ja
Granted legal-status Critical Current

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  • Moulding By Coating Moulds (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
  • Artificial Filaments (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Treatments Of Macromolecular Shaped Articles (AREA)

Abstract

PURPOSE:To get monoaxial orientated total aromatic copoly-imide molded material of high strength, high coefficient elasticity and excellent heat resistance by a method wherein integrity aromatic diamine is reacted with specific mixture of aromatic tetracarboxylic acid dianhydrous compound. CONSTITUTION:Mixtures of integrity aromatic diamine (for instance, p-phenylene diamine, 2,7-diaminofluorene, 2,6-diamino naphtalene) and pyromellitic anhydride with molar ratio 90/10-20/80 and 3,3',4,4'-diphenyl ether tetra carboxylic acid dianhydrous compound are isomolar reacted and are made into polyamid acid, and the desired monoaxial orientated molded material is made by cyclizing to imido group. When it is made into fibers the strength is above 10g/d and the coefficient of elasticity is above 900g/d. It is useful for resin reinforcing fiber or laminated material.

Description

【発明の詳細な説明】 本発明は高強度、高弾性率であり、しかも耐熱性の極め
て高い、−軸配向した全芳香族コポリイミド成型物に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a -axis-oriented wholly aromatic copolyimide molded product which has high strength, high modulus of elasticity, and extremely high heat resistance.

全芳香族ポリイミドは有機ポリマのなかで最高の耐熱性
を有しており、その特徴を生かしてすでにフィルムや成
型物で実用化されている。しかしながら、それらの引張
特性はごくありふれたものであり、強度および弾性率は
決して高くない。高弾性率のポリイミド成型品を得た例
として、Il緒では、特公昭57−37687に剛直性
芳香族ジアミンと特定の芳香族テトラカルボン酸二無水
物からなるポリアミド酸の溶液を湿式紡糸、延伸後、加
熱してイミド基に環化させる方法が開示されている。本
発明者らは高強度、高弾性率かつ耐熱性の極めてよい、
繊維、フィルム、テープなどの一軸配向した成型物を目
標に鋭意検討した結果、剛直性芳香族ジアミンあるいは
その混合物と2種類の特定の芳香族テトラカルボン酸二
無水物の混合物からなる全芳香族ロポリイミドがこの目
的に適していることを見出し、本発明に到達した。
Fully aromatic polyimide has the highest heat resistance among organic polymers, and has already been put to practical use in films and molded products by taking advantage of this characteristic. However, their tensile properties are very common, and their strength and modulus are not high. As an example of obtaining a polyimide molded product with a high elastic modulus, in Japanese Patent Publication No. 57-37687, a solution of polyamic acid consisting of a rigid aromatic diamine and a specific aromatic tetracarboxylic dianhydride was wet-spun and stretched. A method is disclosed in which the compound is then cyclized into an imide group by heating. The present inventors have developed a method that has high strength, high modulus of elasticity, and extremely good heat resistance.
As a result of intensive research aimed at producing uniaxially oriented molded products such as fibers, films, and tapes, we developed a fully aromatic compound consisting of a rigid aromatic diamine or a mixture thereof and a mixture of two specific aromatic tetracarboxylic dianhydrides. We have discovered that polyimide is suitable for this purpose and have arrived at the present invention.

本発明の成型物は、鎖伸長結合が同軸かほぼ同軸もしく
は平行で逆向きに伸びている芳香族ジアミンあるいはそ
の混合物と無水ビ0メリトII(A>および3.3′、
4.4′−ジフェニルエーテルテトラカルボン酸二無水
物(B)からなり、Al6(モル比)が90/10〜2
0/80である、−軸配向した全芳香族コポリイミド成
型物である。
The molded product of the present invention comprises an aromatic diamine or a mixture thereof in which the chain extension bonds are coaxial, nearly coaxial, or parallel and extend in opposite directions, and anhydrous Biomellito II (A> and 3.3',
4. Consisting of 4'-diphenyl ether tetracarboxylic dianhydride (B), Al6 (molar ratio) is 90/10 to 2
It is a fully aromatic copolyimide molded product with a -axis orientation of 0/80.

本発明のコポリイミド成型物は、繊維の場合を例にとる
と10q/d以上の強度、900G/d以上の弾性率を
有しており、また、耐熱性、耐薬品性も極めて高く、多
くの用途に有用である。
Taking the case of fiber as an example, the copolyimide molded product of the present invention has a strength of 10 q/d or more and an elastic modulus of 900 G/d or more, and also has extremely high heat resistance and chemical resistance, and has many Useful for applications such as

以下、本発明をさらに詳細に説明する。本発明の全芳香
族コポリイミドは一旦、つくってしまうともはや溶融し
ないし、また、溶剤もない。そこで、有機溶剤に可溶な
前駆重合体であるポリアミド酸をまずつくり、ついで賦
型加工した後、適当な手段を用いてイミド基に環化させ
ねばならない。
The present invention will be explained in more detail below. Once the wholly aromatic copolyimide of the present invention is made, it no longer melts and there are no solvents. Therefore, it is necessary to first prepare a polyamic acid precursor which is soluble in an organic solvent, then to shape it, and then to cyclize it into an imide group using an appropriate means.

したがって、まず、ポリアミド酸の製造方法について説
明する。本発明で用いる芳香族ジアミンは鎖伸長結合が
同軸かほぼ同軸もしくは平行で逆向きに伸びている、い
わゆる剛直構造のジアミンでベンジジン、2.2′−ジ
クロルベンジジン、4.4″−ジアミノ−p−ターフェ
ニルなどがある。
Therefore, first, the method for producing polyamic acid will be explained. The aromatic diamine used in the present invention has a so-called rigid structure in which the chain extending bonds are coaxial, almost coaxial, or parallel and extend in opposite directions, such as benzidine, 2,2'-dichlorobenzidine, and 4.4''-diamino- Examples include p-terphenyl.

はぼ同軸型の例としては2.7−ジアミツフルオレン、
2.7−ジアミツフルオレノン、2.7−ジアミツジベ
ンゾフランが挙げられる。また、平行型としては2.6
−ジアミノナフタリン、1.5−ジアミノナフタリンな
どがある。これらのジアミンは単独あるいは2種以上の
混合物として重合に供する。一方、酸無水物としては無
水ピロメリトm (A)および3.3′、4.4′−ジ
フェニルエーテルテトラカルボン酸二無水物(B)を用
いる。A/8 (モル比)は90/10〜20/80で
あり、この範囲外では比較例で示すように高性能の成型
物が得られない。
Examples of the coaxial type are 2,7-diamitsufluorene,
Examples thereof include 2,7-diamitfluorenone and 2,7-diamitudibenzofuran. Also, as a parallel type, 2.6
-diaminonaphthalene, 1,5-diaminonaphthalene, etc. These diamines may be used alone or as a mixture of two or more for polymerization. On the other hand, as the acid anhydride, pyromellitic anhydride (A) and 3.3',4.4'-diphenyl ether tetracarboxylic dianhydride (B) are used. A/8 (molar ratio) is 90/10 to 20/80, and outside this range, a high-performance molded product cannot be obtained as shown in the comparative example.

上記のジアミンもしくはジアミン混合物をアミド系溶媒
に溶解させ、ついでジアミン成分と実質的に等モルの上
述の酸無水物の混合物を加えて重縮合させると、前駆重
合体であるポリアミド酸の溶液が得られる。重合に用い
るアミド系゛溶媒としてはN−メチルピロリドン(NM
P)、N1N−ジメチルアセトアミド、N、N−ジメチ
ルホルムアミドなどがある。
By dissolving the above diamine or diamine mixture in an amide solvent, and then adding and polycondensing the mixture of the above acid anhydrides in substantially equimolar amounts to the diamine component, a solution of polyamic acid, which is a precursor polymer, is obtained. It will be done. As the amide solvent used for polymerization, N-methylpyrrolidone (NM
P), N1N-dimethylacetamide, N,N-dimethylformamide, and the like.

かくして得たポリアミド酸の溶液を用いてつぎに繊維、
フィルム、テープなどに成型する。その方法は大別して
湿式法と乾式法があるが、まず、湿式法から説明する。
Using the polyamic acid solution thus obtained, fibers,
Molded into films, tapes, etc. The methods can be broadly divided into wet methods and dry methods, but the wet method will be explained first.

湿式法で用いる原液は上記のポリアミド酸溶液そのもの
でもよいが、本発明者らが先に特願昭58−27068
で提案した、アミド酸単位の一部を化学環化剤を使って
溶液中で環化させた、部分環化ポリマ溶液を用いる方が
透明な、ボイドのない湿式成型物を与えるのでより好ま
しい。かかる環化剤としては無水酢酸、無水プロピオン
酸などの脂肪族酸無水物が適している。その添加量はア
ミド酸単位に対して約0.1当量〜0.4当量である。
The stock solution used in the wet method may be the above-mentioned polyamic acid solution itself, but the present inventors have previously proposed
It is more preferable to use a partially cyclized polymer solution, in which a part of the amic acid units are cyclized in solution using a chemical cyclizing agent, as proposed in 2007, as it provides a transparent, void-free wet molded product. As such a cyclizing agent, aliphatic acid anhydrides such as acetic anhydride and propionic anhydride are suitable. The amount added is about 0.1 equivalent to 0.4 equivalent relative to the amic acid unit.

この化学環化にはピリジン、3−メチルピリジン、3.
5−ルチジン、キノリンなどの有機塩基を触媒として用
いてもよい。その添加量は特に限定されない。
This chemical cyclization includes pyridine, 3-methylpyridine, 3.
Organic bases such as 5-lutidine and quinoline may be used as catalysts. The amount added is not particularly limited.

上記のポリアミド酸溶液あるいはアミド酸の一部をイミ
ド基に環化させたポリマ溶、液をオリフィス、スリット
ダイなどを通じて水系凝固浴中に押し出す。あるいは平
面の板の上に流延して水系凝固浴中に浸漬する。凝固浴
としては水、重合溶媒の水溶液あるいは無機塩の水溶液
のいずれでもよ5− いが、重合溶媒の回収の容易さからみて、同じ溶媒の水
溶液がもっとも好ましい、凝固浴温度は0〜50℃が適
当である。凝固した成型物は引続いて延伸してもよい。
The above polyamic acid solution or a polymer solution in which a portion of the amic acid is cyclized into imide groups is extruded into an aqueous coagulation bath through an orifice, a slit die, or the like. Alternatively, it is cast onto a flat plate and immersed in an aqueous coagulation bath. The coagulation bath may be water, an aqueous solution of a polymerization solvent, or an aqueous solution of an inorganic salt, but from the viewpoint of ease of recovery of the polymerization solvent, an aqueous solution of the same solvent is most preferable, and the coagulation bath temperature is 0 to 50°C. is appropriate. The solidified molding may subsequently be stretched.

この延伸は水洗を兼ねて水中で行なってもよいし、また
空気中で延伸してもかまわない。延伸温度は10〜90
℃が好適であり、また延伸倍率は1.2〜3.0倍であ
る。
This stretching may be carried out in water, which also serves as washing, or may be carried out in air. Stretching temperature is 10-90
℃ is suitable, and the stretching ratio is 1.2 to 3.0 times.

未延伸あるいは延伸した凝固成型物はそのまま乾燥し、
ついで熱環化に供するか、あるいは膨潤したまま化学環
化剤で処理しアミド酸をイミド基に閉環させる。後者の
場合に用いる環化剤および触媒は、上記の溶液中での部
分環化に使用する薬品と同じであり、特に無水酢酸−ピ
リジンの組み合わせが好適である。なお、凝固成型物を
化学環化させる前に、活性水素をもたない、水と混ざる
有機溶剤で洗って成型物中の水を抽出除去してもよい。
The unstretched or stretched solidified molded product is dried as it is,
Then, it is subjected to thermal cyclization or treated with a chemical cyclizing agent while swollen to close the amic acid to an imide group. The cyclizing agent and catalyst used in the latter case are the same as those used for the partial cyclization in solution, and the combination of acetic anhydride and pyridine is particularly suitable. Note that, before chemically cyclizing the solidified molded product, water in the molded product may be extracted and removed by washing with an organic solvent that does not contain active hydrogen and is miscible with water.

かかる溶剤としてアセトン、テトラヒドロフラン、ジオ
キサンなどが適している。また、化学環化時に他の有機
溶剤を希釈剤として用いてもよい。かかる希釈剤として
はジオキサン、ベンゼ6一 ン、トルエン、クロロホルム、四塩化炭素、アセトニト
リルなどがある。化学環化の処理条件は温度15〜50
℃、また、処理時間は10分から1日あるいはそれ以上
である。化学環化させた成型物はつぎに乾燥するが、そ
の前に環化剤を除去すべく有機溶剤で洗ってもよい。か
かる洗浄剤とし空乾燥あるいは加熱ドラムなどを用いる
連続式乾、燥のいずれを採用してもよい。
Suitable solvents include acetone, tetrahydrofuran, dioxane, and the like. Further, other organic solvents may be used as diluents during chemical cyclization. Such diluents include dioxane, benzene, toluene, chloroform, carbon tetrachloride, acetonitrile, and the like. Chemical cyclization treatment conditions are temperature 15-50
℃, and the treatment time ranges from 10 minutes to 1 day or more. The chemically cyclized molded product is then dried, but before drying, it may be washed with an organic solvent to remove the cyclizing agent. As such a cleaning agent, either air drying, continuous drying using a heated drum, or drying may be employed.

・:1 (乾燥した成型物は最後に熱延伸もしくは熱処理、Iこ
供する。化学環化させていない成型物はこの■1.程で
アミド酸がイミド基に熱環化する。ポリアミド酸の成型
物の段階で延伸していない場合は、この工程で必ず延伸
しなければならない。その手段としては熱板あるいは加
熱筒のいずれを用いてもよい。また、熱延伸もしくは熱
処理は段階的に温度を上げて実施してもよく、温度は最
終的に400℃以上が好ましい。また、その雰囲気は空
気あるいは窒素などの不活性ガスである。
・:1 (The dried molded product is finally subjected to hot stretching or heat treatment.For molded products that have not been chemically cyclized, the amic acid is thermally cyclized to imide groups in step 1. Molding of polyamic acid. If the product is not stretched at the product stage, it must be stretched in this step. Either a hot plate or a heating tube may be used as a means for stretching. Also, hot stretching or heat treatment involves increasing the temperature in stages. The final temperature is preferably 400° C. or higher, and the atmosphere is air or an inert gas such as nitrogen.

つぎに乾式成型について説明する。この場合も重合して
得たポリアミド酸溶液をそのまま原液に用いる方法と、
実質的に環化が起こらないような温度条件(10℃以下
)で化学環化剤を加えたポリマ溶液を用いる方法がある
。後者の場合、フィルムなどの形状に成型後、環化が起
こる温度に上げてゲル化させ、形態保持性を与える。用
いる化学環化剤は湿式成型の部で述べたものと同じであ
り、その添加量はアミド酸当量に対し1.5〜3゜押し
出してフィルム状に成型することができる。
Next, dry molding will be explained. In this case as well, there is a method of using the polyamic acid solution obtained by polymerization as the stock solution as it is,
There is a method of using a polymer solution to which a chemical cyclizing agent is added under temperature conditions (10° C. or lower) where cyclization does not substantially occur. In the latter case, after being molded into a shape such as a film, the temperature is raised to a temperature at which cyclization occurs to cause gelation and form retention. The chemical cyclizing agent used is the same as that described in the wet molding section, and the amount added can be extruded by 1.5 to 3° relative to the amic acid equivalent to form a film.

ついで温度を上げて溶媒を蒸発させるとともに熱□環化
を進める。化学環化剤を加えた溶液の場合に茅 、また、ポリアミド酸溶液を口金を通じて高温の空気流
中に吐出し繊維をつくることもできる。かくして得た繊
維、フィルムなどの成型物はついで延伸しなければなら
ない。延伸は溶媒の一部が残っている状態で実施しても
よいし、また、溶媒を完全に蒸発させた後、行なっても
よい。一般には、前者の方がより低温で延伸可能なので
操作上やりやすい。この熱延伸および熱処理の方法は既
述の湿式成型物の場合とまったく同じである。
Then, the temperature is raised to evaporate the solvent and proceed with thermal cyclization. In the case of a solution containing a chemical cyclizing agent, fibers can also be produced by discharging a polyamic acid solution into a hot air stream through a die. The thus obtained molded articles, such as fibers and films, must then be stretched. Stretching may be carried out with a portion of the solvent remaining, or may be carried out after the solvent has been completely evaporated. Generally, the former method is easier to operate because it can be stretched at a lower temperature. The hot stretching and heat treatment methods are exactly the same as those for the wet molded product described above.

本発明の一軸配向した全芳香族コポリイミド成型物は、
繊維を例にとるとm1flOq/d以上、弾性率900
C1/d以上と極めて高性能であり、耐熱性、耐薬品性
も非常にすぐれている。したがって多くの用途に有用で
あり、たとえば、ゴム、樹脂などの補強用、耐熱電絶用
途などに用いられる。また、積層したテープを構造材に
用いることMPで希釈して25℃で測定したものである
The uniaxially oriented wholly aromatic copolyimide molded product of the present invention is
Taking fiber as an example, m1flOq/d or more, elastic modulus 900
It has extremely high performance with C1/d or higher, and has excellent heat resistance and chemical resistance. Therefore, it is useful for many uses, such as reinforcing rubber, resin, etc., and heat-resistant insulation. In addition, the laminated tape was diluted with MP and measured at 25° C. when used as a structural material.

9− リ、試長100mm、引張速度20 mm/ 1lli
n 0また、゛フィルムは試長25mm、引張速度10
作/minで測定した。
9-li, sample length 100mm, tensile speed 20mm/1lli
n 0 Also, the film has a trial length of 25 mm and a tensile speed of 10
It was measured in terms of work/min.

・II 実施例1 本実施例はジアミン成分がベンジジン、酸無水物成分が
無水ピロメリト酸(PMDA)40モル%、3.3′4
.4′−ジフェニルエーテルテトラカルボン酸二無水物
(DEDA)60モル%からなるコポリイミド繊維の製
糸結果を示す。
・II Example 1 In this example, the diamine component was benzidine, and the acid anhydride component was pyromellitic anhydride (PMDA), 40 mol%, 3.3'4
.. The results of spinning a copolyimide fiber containing 60 mol% of 4'-diphenyl ether tetracarboxylic dianhydride (DEDA) are shown.

脱水したNMPloomlにベンジジン6.55Qを溶
解させ、乳鉢でよく粉砕して混合したPMDA3.12
GおよびDEDA6.650を加えて重合させ、η1n
h2.38のポリアミド酸の溶液を得た(ポリマ濃度1
4.0%)。
PMDA3.12 was prepared by dissolving benzidine 6.55Q in dehydrated NMProom, grinding it well in a mortar, and mixing it.
G and DEDA6.650 were added and polymerized, η1n
A solution of polyamic acid with h2.38 was obtained (polymer concentration 1
4.0%).

このポリアミド酸の溶液を氷水で冷却し、攪拌下に無水
酢酸1.46Q、ピリジン1.13(1(いずれもアミ
ド酸単位の0.2当量)およびNMP17+alからな
る混合物を30分で滴下し、つ10− いで25℃で5時間反応を続けた。得られた部分環化ポ
リアミド酸溶液はポリマ濃度12.0%、ついで25℃
の水中で1.4倍に延伸した。この凝固糸条を無水酢酸
/ピリジン(容量比70/30)中に室温で一夜浸漬し
、残りのアミド酸を化、゛ 学理化させた。この化学環
化糸をトルエンに90分浸漬後、巻直しで真空乾燥した
。ついで、窒素をゆるく通、じた、長さ30cn+のガ
ラス製円筒管を用い、550℃で6.5倍に熱延伸した
く給糸速113、 On+ /min )。この熱延伸
糸の糸質は繊度7.3デニール、強度19.5q/d、
伸度1゜7%、弾性率1274a/dと高性能であった
This polyamic acid solution was cooled with ice water, and while stirring, a mixture consisting of 1.46Q acetic anhydride, 1.13Q pyridine (1 (both 0.2 equivalents of amic acid unit) and NMP17+al was added dropwise over 30 minutes, The reaction was continued at 25°C for 5 hours at 10°C.The resulting partially cyclized polyamic acid solution had a polymer concentration of 12.0%, and then at 25°C.
The film was stretched 1.4 times in water. The coagulated thread was immersed in acetic anhydride/pyridine (volume ratio 70/30) overnight at room temperature to chemically dissolve the remaining amic acid. This chemically cyclized yarn was immersed in toluene for 90 minutes, then re-wound and vacuum-dried. Then, using a glass cylindrical tube with a length of 30 cm+ through which nitrogen was gently passed, the material was hot-stretched to 6.5 times at 550° C. (fiber feeding speed 113, On+/min). The yarn quality of this hot drawn yarn is a fineness of 7.3 denier, a strength of 19.5 q/d,
It had high performance with an elongation of 1.7% and an elastic modulus of 1274 a/d.

この延伸糸をさらに窒素雰囲気下、525℃で6秒間、
緊張熱処理した後は、強度19.70/d1伸度1.7
%、弾性率1310q/dであり、若干の性能向上がみ
られた。
This drawn yarn was further heated at 525°C for 6 seconds under a nitrogen atmosphere.
After tension heat treatment, strength: 19.70/d1 elongation: 1.7
%, and the elastic modulus was 1310 q/d, indicating a slight improvement in performance.

比較例1 本比較例はベンジジンとPMDAからなるホモポリイミ
ド繊維の製糸結果を示す。
Comparative Example 1 This comparative example shows the results of spinning homopolyimide fibers made of benzidine and PMDA.

NMP中でベンジンとPMDAを反応させ、ボリア11
度6.0%、η1nh5.74、溶液粘度8550 p
oiseのポリアミド酸溶液を得た。この溶液の一部を
とり実施例1とほぼ同じ処方で、アミド酸単位の0.1
5当量の無水酢酸およびピリジン、さらに適当量のNM
Pを加え、ポリマ濃度4゜0%、溶液粘度93 Q p
oiseの部分環化ポリアミド酸溶液をつくった。
By reacting benzine and PMDA in NMP, boria 11
degree 6.0%, η1nh5.74, solution viscosity 8550p
A polyamic acid solution of oise was obtained. A portion of this solution was prepared using almost the same recipe as in Example 1, and 0.1 of the amic acid unit was added.
5 equivalents of acetic anhydride and pyridine, plus an appropriate amount of NM
Add P, polymer concentration 4°0%, solution viscosity 93 Q p
A partially cyclized polyamic acid solution of oise was prepared.

゛この溶液を実施例1と同じ装置および処方を用いて湿
式紡糸し、水中で1.4倍に延伸後、無水酢酸/ピリジ
ン(70/30)に室温で一夜浸漬し、化学環化させた
。ついで、真空乾燥し、窒素雰囲気で熱延伸を試みたが
、600℃でも1.03倍に延伸されるにすぎず、糸質
も繊度14.0デニール、強度7.70/d、伸度1.
0%、弾性率877 o/dと実施例1の繊維にくらべ
て相当劣っていた。
゛This solution was wet-spun using the same equipment and recipe as in Example 1, stretched to 1.4 times in water, and then immersed in acetic anhydride/pyridine (70/30) overnight at room temperature for chemical cyclization. . Next, I tried vacuum drying and hot stretching in a nitrogen atmosphere, but the stretching was only 1.03 times even at 600°C, and the yarn quality was 14.0 denier, strength 7.70/d, and elongation 1. ..
0% and an elastic modulus of 877 o/d, which was considerably inferior to the fiber of Example 1.

比較例2 本比較例はベンジジンとDEDAからなるホモポリイミ
ド繊維の製糸結果を示す。
Comparative Example 2 This comparative example shows the results of spinning homopolyimide fibers made of benzidine and DEDA.

NMP中でベンジジンとDEDAを反応させ、ポリv1
1度15.1%、η1nh1.70のポリアミド酸溶液
をつくり、ついでアミド酸単位の0゜17当量の無水酢
酸およびピリジン、さらに適当量のNMPを添加してポ
リマ濃度14.1%、溶液粘度460 poiseの部
分環化ポリマ溶液を得た。
By reacting benzidine and DEDA in NMP, polyv1
A polyamic acid solution with a concentration of 15.1% and η1nh of 1.70 was prepared, and then acetic anhydride and pyridine in an amount of 0.17 equivalents of the amic acid unit, and an appropriate amount of NMP were added to give a polymer concentration of 14.1% and a solution viscosity. A partially cyclized polymer solution of 460 poise was obtained.

この溶液を実施例1と同じ処方で湿式紡糸し、室温の水
中で1.44倍に延伸後、室温の無水酢糸の糸質は繊度
18.4デニール、強度10.7□6 / d 、伸度
1.8%、弾性率713 o/dであ実施例2 本実施例はベンジジン、PMDAおよびDED13− Aからなる、本発明の範囲内のいくつかのコポリイミド
5illIの製糸結果を示す。重合、溶液中の部分環化
、湿式紡糸、凝固糸の化学環化および熱延伸の処方は実
施例1とほぼ同じである。結果を表1に一括して記した
。どのfiAHも比較例1.2の繊維より強度および弾
性率が高い。
This solution was wet-spun using the same formulation as in Example 1, and after being stretched 1.44 times in water at room temperature, the anhydrous vinegar yarn at room temperature had a fineness of 18.4 denier and a strength of 10.7□6/d. Example 2 This example shows the spinning results of several copolyimides within the scope of the present invention, 5illI, consisting of benzidine, PMDA and DED13-A. The recipes for polymerization, partial cyclization in solution, wet spinning, chemical cyclization of coagulated yarn, and hot stretching are almost the same as in Example 1. The results are summarized in Table 1. All fiAHs have higher strength and modulus than the fibers of Comparative Example 1.2.

14− 表1 実施例3 NMP中で2−クロルベンジジン、PMDA(70モル
%)、DEDA (30モル%)を重合させ、ポリマ濃
度17.0%、η1nh1.71(7)ポリアミド酸溶
液を得た。ついで実施例1と同じ処方で無水酢酸および
ピリジン(いずれもアミド酸単位の0.2当量)さらに
少量のNMPを添加し、ポリマ濃度15.7%、溶液粘
度29801)Oiseの部分環化ポリマ溶液をつくっ
た。
14- Table 1 Example 3 2-Chlorbenzidine, PMDA (70 mol%), and DEDA (30 mol%) were polymerized in NMP to obtain a polyamic acid solution with a polymer concentration of 17.0% and η1nh1.71 (7). Ta. Next, acetic anhydride and pyridine (both 0.2 equivalents of the amic acid unit) were added to the same recipe as in Example 1, and a small amount of NMP was added to prepare a partially cyclized polymer solution of Oise (polymer concentration: 15.7%, solution viscosity: 29801). I made it.

この溶液を実施例1と同じ装置および手法で湿式紡糸し
、無水酢酸/ピリジン(70/30 )中に室温で一夜
浸漬し化学環化させた。ついで真空乾燥後、窒素雰囲気
下、550℃で4.2倍に熱延伸して得た1111の糸
質は繊度17.0デニール、強度17.00/d、伸度
1.9%、弾性率1066 o/dであった。
This solution was wet-spun using the same equipment and method as in Example 1, and was immersed in acetic anhydride/pyridine (70/30) overnight at room temperature for chemical cyclization. After vacuum drying, the yarn quality of 1111 obtained by hot stretching 4.2 times at 550° C. in a nitrogen atmosphere has a fineness of 17.0 denier, a strength of 17.00/d, an elongation of 1.9%, and an elastic modulus. It was 1066 o/d.

実施例4 本実施例はジアミン成分がベンジジン30モル%、2.
2′−ジクロルベンジジン70モル%からなり、酸無水
物成分がl)MDA70モル%、DEDA30モル%か
らなるコポリイミド繊維の製糸結果を示す。
Example 4 In this example, the diamine component was 30 mol% of benzidine, 2.
The results of spinning a copolyimide fiber consisting of 70 mol% of 2'-dichlorobenzidine and whose acid anhydride components are 1) 70 mol% of MDA and 30 mol% of DEDA are shown.

加え、ポリマ濃疾15.6%、溶液粘1i1320pO
+ seの部分環化ポリマ溶液を得た。
In addition, polymer concentration 15.6%, solution viscosity 1i 1320pO
+se partially cyclized polymer solution was obtained.

化学環化して得た乾燥糸を窒素雰囲気下、575℃で5
.2倍に熱延伸した。延伸糸の糸質は繊度12.9デニ
ール、強度18.Oq/d、伸度2゜1%、弾性率9.
860/dであった。
The dried yarn obtained by chemical cyclization was heated at 575°C for 5 minutes in a nitrogen atmosphere.
.. It was hot stretched twice. The drawn yarn has a fineness of 12.9 denier and a strength of 18. Oq/d, elongation 2°1%, elastic modulus 9.
It was 860/d.

実施例5 本実施例はジアミン成分が4.4″−ジアミノ−p−タ
ーフェニルであり、酸無水物成分がPM17− DA35モル%およびDEDA65モル%からなるコポ
リイミドm維の製糸結果を示す。
Example 5 This example shows the results of spinning a copolyimide m-fiber in which the diamine component is 4.4''-diamino-p-terphenyl and the acid anhydride component is 35 mol% PM17-DA and 65 mol% DEDA.

上記モノマをNMP中で反応させ、ポリマ濃度17%、
η1nh1.58のポリアミド酸溶液をつくり、アミド
酸単位の0.2当量の無水酢酸およびピリジン、さらに
少量のNMPを加えて部分環化させた。この溶液(ポリ
マ濃度15.6%、溶液粘度2530ρoise )を
実施例1とほぼ同じ手法で湿式紡糸後、化学環化させた
、ついで、真空乾燥後、窒素雰囲気下、550℃で2.
9倍に熱本実施例はジアミン成分がベンジジン、酸無水
物成分がPMDA40モル%、DEDA60モル%から
なるコポリイミドの一軸延伸フィルムの製造例を示す。
The above monomers were reacted in NMP, and the polymer concentration was 17%.
A polyamic acid solution of η1nh1.58 was prepared, and acetic anhydride and pyridine in an amount of 0.2 equivalents of the amic acid unit, as well as a small amount of NMP, were added for partial cyclization. This solution (polymer concentration 15.6%, solution viscosity 2530 ρoise) was wet-spun in substantially the same manner as in Example 1, chemically cyclized, and then dried under vacuum at 550°C under a nitrogen atmosphere.
This example shows the production of a uniaxially stretched copolyimide film in which the diamine component is benzidine and the acid anhydride components are PMDA 40 mol % and DEDA 60 mol %.

実施例1で使用した紡糸原液の残りをとり、ドライアイ
ス−アセトン浴で一10℃に冷却し、攪18− 拌しながらアミド酸単位の2.0当量の無水酢酸、1.
0当最のピリジンおよび適当量のNMPの混合物を5分
かけて滴下し、さらに10分攪拌を続けた(ポリマ濃度
7.5%)。この溶液をガラス板上に流延し、70℃の
オーブン中で1時間加熱した。得られた化学環化フィル
ムのポリマ濃度は約85%であった。このフィルムをガ
ラス板からはがし、31TITlあるいはllTlT1
幅に切断後、200℃の熱板を用いて1.6倍に延伸し
、さらに400℃の熱板で5秒間、緊張熱処理した。こ
の延伸フィルムを450℃のオーブンに入れ、弛緩状態
で4分間処理した。得られたフィルムの引張特性は以下
のとおりであった。
The remainder of the spinning dope used in Example 1 was taken, cooled to -10°C in a dry ice-acetone bath, and mixed with 2.0 equivalents of amic acid units of acetic anhydride, 1.
A mixture of pyridine and an appropriate amount of NMP was added dropwise over 5 minutes, and stirring was continued for an additional 10 minutes (polymer concentration 7.5%). This solution was cast onto a glass plate and heated in an oven at 70°C for 1 hour. The polymer concentration of the chemically cyclized film obtained was about 85%. Peel off this film from the glass plate and
After cutting to width, it was stretched 1.6 times using a 200°C hot plate, and was further subjected to tension heat treatment for 5 seconds on a 400°C hot plate. This stretched film was placed in an oven at 450°C and treated in a relaxed state for 4 minutes. The tensile properties of the obtained film were as follows.

特許出願人 工 業 技 術 院 長 19−Patent applicant: Institute of Technology Director 19-

Claims (1)

【特許請求の範囲】[Claims] 4.4’ −ジフェニルエーテルテトラカルボン酸二無
水物(B)からなり、Al6 (モル比)が90/10
〜20/80である、−軸配向した全芳香族コポリイミ
ド成型物。
4. Consisting of 4'-diphenyl ether tetracarboxylic dianhydride (B), Al6 (molar ratio) is 90/10
~20/80 -axis oriented wholly aromatic copolyimide molded product.
JP58205779A 1983-11-04 1983-11-04 Monoaxially orientated total aromatic copolyimide molded material Granted JPS6097834A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58205779A JPS6097834A (en) 1983-11-04 1983-11-04 Monoaxially orientated total aromatic copolyimide molded material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58205779A JPS6097834A (en) 1983-11-04 1983-11-04 Monoaxially orientated total aromatic copolyimide molded material

Publications (2)

Publication Number Publication Date
JPS6097834A true JPS6097834A (en) 1985-05-31
JPH036174B2 JPH036174B2 (en) 1991-01-29

Family

ID=16512527

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58205779A Granted JPS6097834A (en) 1983-11-04 1983-11-04 Monoaxially orientated total aromatic copolyimide molded material

Country Status (1)

Country Link
JP (1) JPS6097834A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62214927A (en) * 1986-03-14 1987-09-21 Ube Ind Ltd Polyimide orienting molded product of high physical properties and manufacture of same
JPS6420238A (en) * 1987-07-15 1989-01-24 Kanegafuchi Chemical Ind Production of aromatic polyimide polymer molding

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62214927A (en) * 1986-03-14 1987-09-21 Ube Ind Ltd Polyimide orienting molded product of high physical properties and manufacture of same
JPS6420238A (en) * 1987-07-15 1989-01-24 Kanegafuchi Chemical Ind Production of aromatic polyimide polymer molding

Also Published As

Publication number Publication date
JPH036174B2 (en) 1991-01-29

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