JPH0733872A - Production of polyimide precursor powder - Google Patents

Production of polyimide precursor powder

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Publication number
JPH0733872A
JPH0733872A JP20276393A JP20276393A JPH0733872A JP H0733872 A JPH0733872 A JP H0733872A JP 20276393 A JP20276393 A JP 20276393A JP 20276393 A JP20276393 A JP 20276393A JP H0733872 A JPH0733872 A JP H0733872A
Authority
JP
Japan
Prior art keywords
polyimide precursor
powder
solvent
polyimide
precursor powder
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
JP20276393A
Other languages
Japanese (ja)
Inventor
Mikio Furukawa
幹夫 古川
Isao Tomioka
功 富岡
Yoshiaki Iwaya
嘉昭 岩屋
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.)
Unitika Ltd
Original Assignee
Unitika 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 Unitika Ltd filed Critical Unitika Ltd
Priority to JP20276393A priority Critical patent/JPH0733872A/en
Publication of JPH0733872A publication Critical patent/JPH0733872A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To easily obtain the subject powder having high polymerization degree and excellent mechanical properties and useful for a molded article having low residual solvent content by polymerizing a tetracarboxylic acid dianhydride with a diamine in a water-soluble nitrile compound as an easily removable reaction solvent. CONSTITUTION:This powder is produced by dissolving or suspending a tetracarboxylic acid dianhydride in a water-soluble nitrile compound (preferably acetonitrile), adding a diamine, polymerizing at -20 to +50 deg.C (especially preferably 0-20 deg.C) and removing the solvent from the polymer.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、ポリイミド前駆体粉粒
体の製造方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a polyimide precursor powder or granular material.

【0002】[0002]

【従来の技術】従来、例えば、代表的なポリイミド前駆
体であるポリアミド酸は、N,N−ジメチルホルムアミ
ド、N−メチル−2−ピロリドン、ヘキサメチルホスホ
ルアミド、N−メチルカプロラクタム、ジメチルスルホ
キシド、N−アセチル−2−ピロリドン、N,N−ジメ
チルアセトアミド等ポリアミド酸と強く溶媒和する、い
わゆる非プロトン系極性溶媒中で、低温溶液重合方法で
製造されてきた。
Conventionally, for example, polyamic acid which is a typical polyimide precursor is N, N-dimethylformamide, N-methyl-2-pyrrolidone, hexamethylphosphoramide, N-methylcaprolactam, dimethylsulfoxide, It has been produced by a low temperature solution polymerization method in a so-called aprotic polar solvent that strongly solvates with polyamic acids such as N-acetyl-2-pyrrolidone and N, N-dimethylacetamide.

【0003】特公昭39−22196号公報、特公昭3
9−30060号公報、特開昭60−221425号公
報、特開昭61−234号公報、特開昭61−2500
30号公報、特開平2−18420号公報には、ポリイ
ミド前駆体の非プロトン系極性溶媒溶液にアセトン、酢
酸エチルのような貧溶媒と無水酢酸、ピリジンのような
閉環剤を加え、ポリイミド粉粒体を得る方法や、ポリイ
ミド前駆体の非プロトン系極性溶媒溶液とアセトンやハ
ロゲン化炭化水素とを混合しポリイミド前駆体の粉粒体
を得る方法が開示されている。しかし、これらの製造方
法においては、溶媒の除去が難しく、得られるポリイミ
ド粉粒体やポリイミド前駆体の粉粒体からは、特別な成
形法を用いなければ良好な成形体を得ることができない
等という問題点を有していた。
Japanese Patent Publication No. 39-22196, Japanese Patent Publication No. 3
9-30060, JP-A-60-212425, JP-A-61-234, and JP-A-61-2500.
No. 30 and JP-A No. 2-18420, polyimide powder particles are prepared by adding a poor solvent such as acetone and ethyl acetate and a ring-closing agent such as acetic anhydride and pyridine to an aprotic polar solvent solution of a polyimide precursor. There is disclosed a method for obtaining a polyimide precursor and a method for obtaining a polyimide precursor powder by mixing an aprotic polar solvent solution of a polyimide precursor with acetone or a halogenated hydrocarbon. However, in these production methods, it is difficult to remove the solvent, and from the obtained polyimide powder particles or polyimide precursor powder particles, a good molded product cannot be obtained unless a special molding method is used. Had the problem.

【0004】また、これら問題点を解決する方法とし
て、テトラヒドロフランのような低沸点で、溶媒除去が
容易な溶媒を使用して重合を行い、ポリイミド前駆体粉
粒体を生成させる方法が知られている(工業化学雑誌,
71巻,9号,1559〜1564頁,1968年,J.Appl.Polymer S
ci.,vol.11,609〜627,1967年)。この方法によれば、確
かに、ポリイミド前駆体と強く溶媒和するような非プロ
トン系極性溶媒を含有しないポリイミド前駆体粉粒体が
得られるが、その重合度は低く、高々0.5〜0.6程
度の固有粘度のものしか得られず、そのポリイミド成形
体は充分な力学的特性が得られないという問題点があっ
た。
As a method for solving these problems, a method is known in which polymerization is carried out using a solvent having a low boiling point, such as tetrahydrofuran, which can be easily removed, to produce a polyimide precursor powder. (Industrial Chemistry Magazine,
Volume 71, Issue 9, 1559-1564, 1968, J. Appl. Polymer S
ci., vol.11,609-627,1967). According to this method, it is possible to obtain a polyimide precursor powder which does not contain an aprotic polar solvent which strongly solvates with the polyimide precursor, but the degree of polymerization thereof is low and is 0.5 to 0 at most. There is a problem that only polyimide having an intrinsic viscosity of about 0.6 can be obtained, and the polyimide molded body cannot obtain sufficient mechanical properties.

【0005】[0005]

【発明が解決しようとする課題】そこで、本発明の課題
は、溶媒除去が容易で、重合度の高いポリイミド前駆体
の粉粒体を得ることができるポリイミド前駆体の粉粒体
の製造方法を提供することにある。
SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide a method for producing a polyimide precursor powder which can easily remove a solvent and obtain a polyimide precursor powder having a high degree of polymerization. To provide.

【0006】[0006]

【課題を解決するための手段】本発明者らは、上記課題
を解決すべく鋭意検討した結果、水溶性ニトリル類中で
テトラカルボン酸二無水物とジアミンを重合すると、溶
媒との相互作用が少なく、また、その高い蒸気圧とも相
まって溶媒除去が容易であり、固有粘度0.7以上であ
るポリイミド前駆体の粉粒体が得られ、また、このポリ
イミド前駆体は成形性に優れ、得られる成形体は、力学
的特性が優れ、残留溶媒が皆無であるという知見を得、
かかる知見に基づいて本発明に到達した。
Means for Solving the Problems As a result of intensive studies to solve the above problems, the present inventors have found that when a tetracarboxylic dianhydride and a diamine are polymerized in a water-soluble nitrile, an interaction with a solvent occurs. The amount of the polyimide precursor is small and, in combination with the high vapor pressure, makes it easy to remove the solvent, and a polyimide precursor powder having an intrinsic viscosity of 0.7 or more is obtained. Further, this polyimide precursor is excellent in moldability and can be obtained. We obtained the knowledge that the molded product has excellent mechanical properties and no residual solvent,
The present invention has been accomplished based on such findings.

【0007】すなわち、本発明の要旨は、水溶性ニトリ
ル類中でテトラカルボン酸二無水物とジアミンを重合す
ることを特徴とするポリイミド前駆体の粉粒体の製造方
法である。
That is, the gist of the present invention is a method for producing powdery particles of a polyimide precursor characterized by polymerizing tetracarboxylic dianhydride and diamine in a water-soluble nitrile.

【0008】以下本発明について詳細に説明する。本発
明において、ポリイミド前駆体とは、加熱又は化学作用
により閉環してポリイミドとなり、ポリマー鎖の繰り返
し単位の60モル%以上、好ましくは70モル%以上、
より好ましくは80モル%以上がポリイミド構造となる
有機ポリマーをいい、閉環して非熱可塑性のポリイミド
となるものであればいかなるものでもよい。閉環させる
方法としては、加熱による方法、無水酢酸やピリジンの
ような閉環剤を用いる方法等、従来知られている方法が
適用できる。
The present invention will be described in detail below. In the present invention, the polyimide precursor is cyclized by heating or chemical action to form a polyimide, and is 60 mol% or more, preferably 70 mol% or more of the repeating unit of the polymer chain.
More preferably, 80 mol% or more is an organic polymer having a polyimide structure, and any polymer may be used as long as it forms a non-thermoplastic polyimide by ring closure. As a method of ring-closing, a conventionally known method such as a method by heating or a method using a ring-closing agent such as acetic anhydride or pyridine can be applied.

【0009】本発明において、好ましいポリイミド前駆
体としては全芳香族系のポリイミド前駆体が挙げられ、
特に一般式(1)で表される繰り返し単位を有する芳香
族ポリアミド酸のホモポリマーまたはコポリマーが好ま
しい。
In the present invention, the preferred polyimide precursors include wholly aromatic polyimide precursors,
A homopolymer or copolymer of an aromatic polyamic acid having a repeating unit represented by the general formula (1) is particularly preferable.

【0010】[0010]

【化1】 [Chemical 1]

【0011】ここで、Rは少なくとも1つの炭素6員環
を含む4価の芳香族残基を示し、4価のうちの2価ずつ
は対をなし、炭素6員環内の隣接する炭素原子に結合し
ている。Rの具体例としては次のようなものが挙げられ
る。
Here, R represents a tetravalent aromatic residue containing at least one 6-membered carbon ring, and two of the 4-valent aromatic residues form a pair, and adjacent carbon atoms in the 6-membered carbon ring form a pair. Are bound to. Specific examples of R include the following.

【0012】[0012]

【化2】 [Chemical 2]

【0013】特に、Rとしては次のものが好ましい。Particularly, R is preferably the following.

【0014】[0014]

【化3】 [Chemical 3]

【0015】また、R’は1〜4個の炭素6員環を持つ
2価の芳香族残基を示す。R’の具体例としては次のよ
うなものが挙げられる。
R'represents a divalent aromatic residue having a 1 to 4 carbon 6-membered ring. Specific examples of R'include the following.

【0016】[0016]

【化4】 [Chemical 4]

【0017】[0017]

【化5】 [Chemical 5]

【0018】また、特にR’としては、次のものが好ま
しい。
Further, the following are particularly preferable as R '.

【0019】[0019]

【化6】 [Chemical 6]

【0020】本発明の製造方法によれば、固有粘度
[η]が0.5以上のポリイミド前駆体が得られるが、
成形体の強度や弾性率等の力学的特性を考慮すると0.
7以上とするのが好ましく、1.0以上にするのが特に
好ましい。[η]の値が大きいほど、閉環したときに強
度や弾性率等の特性が良好なものが得られやすい。な
お、[η]は重合体の分子量と直接関係する値であり、
N,N−ジメチルアセトアミド溶媒中でポリイミド前駆
体濃度0.5重量%、30℃で測定する。[η]を計算
するには重合体溶液が標準粘度計の一定容積の毛細管を
流れる時間と溶媒のみが流れる時間を測定することによ
り、次式を使用して計算することができる。ここで、c
はポリイミド前駆体濃度である。
According to the production method of the present invention, a polyimide precursor having an intrinsic viscosity [η] of 0.5 or more can be obtained.
Considering mechanical properties such as strength and elastic modulus of the molded body, it is 0.
It is preferably 7 or more, and particularly preferably 1.0 or more. The larger the value of [η] is, the easier it is to obtain a product having excellent properties such as strength and elastic modulus when closed. [Η] is a value directly related to the molecular weight of the polymer,
It is measured at 30 ° C. in a N, N-dimethylacetamide solvent at a polyimide precursor concentration of 0.5% by weight. [Η] can be calculated by measuring the time for the polymer solution to flow through a constant volume capillary of a standard viscometer and the time for the solvent alone to flow, using the following equation. Where c
Is the polyimide precursor concentration.

【0021】[0021]

【数1】 [Equation 1]

【0022】本発明においては、水溶性ニトリル類にテ
トラカルボン酸二無水物を溶解あるいは懸濁させてお
き、ジアミンを加えて重合させてポリイミド前駆体を得
る。水溶性ニトリル類の中で好ましい溶媒としては、ア
セトニトリル、プロピオニトリル等が挙げられ、好まし
くはアセトニトリルである。また、本発明の効果を損な
わない範囲で、その他の溶媒を混合してもよい。
In the present invention, a tetracarboxylic dianhydride is dissolved or suspended in water-soluble nitriles, and a diamine is added and polymerized to obtain a polyimide precursor. Among the water-soluble nitriles, preferred solvents include acetonitrile and propionitrile, with acetonitrile being preferred. Further, other solvents may be mixed within a range that does not impair the effects of the present invention.

【0023】反応温度は、−20〜50℃、特に0〜2
0℃が好ましい。また、公知のようにテトラカルボン酸
二無水物とジアミンの仕込比は生成するポリイミド前駆
体の重合度に相関しており、高重合度のポリイミド前駆
体を得るには当モル近傍に仕込むことが好ましい。生成
するポリイミド前駆体は、用いた溶媒には溶解せずに、
溶媒中に懸濁状態になっているので、濾過・乾燥などの
通常の方法によって溶媒を除去してポリイミド前駆体の
粉粒体を得る。この際、本発明においては、ポリイミド
前駆体と強く相互作用しない溶媒を用いているので、溶
媒除去が容易であり、通常の乾燥方法でも溶媒を含有し
ないポリイミド前駆体の粉粒体が得られる。
The reaction temperature is -20 to 50 ° C., especially 0 to 2
0 ° C is preferred. Further, as is known, the charging ratio of tetracarboxylic dianhydride and diamine correlates with the degree of polymerization of the polyimide precursor to be generated, and in order to obtain a polyimide precursor with a high degree of polymerization, it is necessary to charge it in the equimolar vicinity. preferable. The resulting polyimide precursor does not dissolve in the solvent used,
Since it is in a suspended state in the solvent, the solvent is removed by a usual method such as filtration and drying to obtain a polyimide precursor powder. At this time, in the present invention, since a solvent that does not strongly interact with the polyimide precursor is used, it is easy to remove the solvent, and a solvent-free polyimide precursor powder is obtained even by a normal drying method.

【0024】また、このとき、溶媒を除去しきらずに、
あるいはポリイミド前駆体の粉粒体を再度溶媒と混合
し、この状態のままで保存することによりポリイミド前
駆体の経時安定性が保たれる。すなわち、ポリイミド前
駆体の粉粒体と、水溶性ニトリル類とよりなる懸濁液で
はポリイミド前駆体の粉粒体の経時安定性が保たれる。
ポリイミド前駆体の粉粒体は、球状、不定形状、繊維状
などのいかなる形状としてもよい。その粒径は100μ
m以下のものを80重量%以上含むものが好ましい。
At this time, the solvent is not completely removed,
Alternatively, the powdery particles of the polyimide precursor are mixed with the solvent again and stored in this state, so that the stability of the polyimide precursor with time is maintained. That is, in a suspension composed of the polyimide precursor powder and the water-soluble nitriles, the stability of the polyimide precursor powder with time is maintained.
The polyimide precursor powder may have any shape such as spherical shape, irregular shape, or fibrous shape. The particle size is 100μ
Those containing 80% by weight or more of m or less are preferable.

【0025】ポリイミド前駆体の粉粒体の成形方法とし
ては、従来公知の方法、すなわち、加熱、加圧すること
により、ポリイミド前駆体の粉粒体を構成するポリイミ
ド前駆体を閉環させるとともに粉粒体を合着・成形して
もよいし、ポリイミド前駆体の一部を閉環させてポリイ
ミドに変換させた後、加熱、加圧して成形してもよい。
As a method for molding the powder particles of the polyimide precursor, a conventionally known method, that is, by heating and pressurizing the polyimide precursor particles constituting the powder particles of the polyimide precursor to ring-close the powder particles, May be bonded and molded, or a part of the polyimide precursor may be ring-closed to be converted into polyimide, and then heated and pressed to mold.

【0026】例えば、前者の場合には、20〜300
℃、500〜5000kg/cm2 で成形した後、30
0〜400℃で真空中もしくは窒素中で焼結して成形体
を得る。また、後者の場合には、ポリイミド前駆体の粉
粒体を150〜200℃において3〜10時間かけてポ
リイミドの粉粒体に変換した後、250〜300℃、5
00〜3000kg/cm2 でプレス成形をして成形体
を得る。ここで、ポリイミド前駆体を閉環する際、閉環
剤の添加量を制御することにより、又は、加熱温度や加
熱時間を制御することにより、ポリイミドへの変換率を
任意に制御することができる。
For example, in the former case, 20 to 300
30 ° C. after molding at 500 to 5000 kg / cm 2
A compact is obtained by sintering at 0 to 400 ° C. in vacuum or in nitrogen. In the latter case, the powder of the polyimide precursor is converted into the powder of polyimide at 150 to 200 ° C. for 3 to 10 hours, and then 250 to 300 ° C.
Press molding is performed at a pressure of 00 to 3000 kg / cm 2 to obtain a molded body. Here, when the polyimide precursor is ring-closed, the conversion rate to polyimide can be arbitrarily controlled by controlling the addition amount of the ring-closing agent, or by controlling the heating temperature and the heating time.

【0027】[0027]

【実施例】以下、実施例により本発明を具体的に説明す
る。なお、各特性値は次のようにして求めた。
EXAMPLES The present invention will be specifically described below with reference to examples. Each characteristic value was obtained as follows.

【0028】(1)粉粒体の粒度:レーザー回折/散乱
式粒度分布測定(堀場製作所製LA−500)にて測定
した。
(1) Particle size of powder and granules: Measured by laser diffraction / scattering type particle size distribution measurement (LA-500 manufactured by Horiba Ltd.).

【0029】(2)イミド化率:赤外吸収スペクトルの
604cm-1と880cm-1の吸光度比(吸光度比0.
804でイミド化率100%とした)から求めた。
(2) Imidization ratio: Absorbance ratio at 604 cm -1 and 880 cm -1 of infrared absorption spectrum (absorbance ratio of 0.
The imidization ratio was 100% at 804).

【0030】(3)表面積:BET吸着法により窒素吸
着量から得られたポリイミド粉粒体グラム当りの平方メ
ートル数である。
(3) Surface area: The number of square meters per gram of polyimide powder granules obtained from the nitrogen adsorption amount by the BET adsorption method.

【0031】(4)強度:ポリイミド粉粒体を成形し
て、曲げ試験(JIS−K7203)にて評価した。
(4) Strength: A polyimide powder was molded and evaluated by a bending test (JIS-K7203).

【0032】実施例1 4.39gのピロメリット酸二無水物(PMDA)およ
び4.01gのジアミノジフェニルエーテル(DAD
E)にアセトニトリル100gを加え、25℃で10時
間攪拌したところ黄色懸濁液が得られた。この懸濁液を
減圧下で濾別し、表1に示すような特性値を有する黄色
のポリイミド前駆体の粉粒体を得た。さらに、これを減
圧下60℃で1時間乾燥した後、180℃で10時間か
けてイミド化を行い、ポリイミド粉粒体を得た(イミド
化率74%)。このポリイミド粉粒体を曲げ試験片作成
用の金型に充填し、300℃に熱したプレス板上で10
00Kg/cm2 の圧力で30分間圧縮成形し、曲げ試
験片を作成し、曲げ試験を行ったところ、密度が1.4
2g/cm3 、曲げ強度860kgf/cm2 、曲げ弾
性率29500kgf/cm2 であった。
Example 1 4.39 g of pyromellitic dianhydride (PMDA) and 4.01 g of diaminodiphenyl ether (DAD)
When 100 g of acetonitrile was added to E) and stirred at 25 ° C. for 10 hours, a yellow suspension was obtained. The suspension was filtered under reduced pressure to obtain a yellow polyimide precursor powder having the characteristic values shown in Table 1. Further, this was dried under reduced pressure at 60 ° C. for 1 hour and then imidized at 180 ° C. for 10 hours to obtain a polyimide powder (imidization ratio 74%). This polyimide powder or granule was filled in a mold for making a bending test piece, and was pressed on a press plate heated to 300 ° C. for 10 minutes.
When a bending test piece was prepared by compression molding at a pressure of 00 Kg / cm 2 for 30 minutes, a bending test was performed, the density was 1.4.
The bending strength was 2 g / cm 3 , the bending strength was 860 kgf / cm 2 , and the bending elastic modulus was 29500 kgf / cm 2 .

【0033】実施例2 アセトニトリル300gを5℃に冷却し、これに26.
3gのPMDAを懸濁させておき、24.0gのDAD
Eを一度に添加し、1時間攪拌し続けた。冷却をやめ、
さらに2時間攪拌し続けたところ黄色懸濁液が得られ
た。この懸濁液を減圧下で濾別し、表1に示すような特
性値を有する黄色のポリイミド前駆体の粉粒体を得た。
さらに、これを実施例1と同様にして、ポリイミド粉粒
体を得た(イミド化率72%)。
Example 2 300 g of acetonitrile was cooled to 5 ° C., and 26.
Suspend 3g of PMDA and add 24.0g of DAD
E was added all at once and stirring was continued for 1 hour. Stop cooling,
When stirring was continued for another 2 hours, a yellow suspension was obtained. The suspension was filtered under reduced pressure to obtain a yellow polyimide precursor powder having the characteristic values shown in Table 1.
Further, a polyimide powder was obtained in the same manner as in Example 1 (72% imidization ratio).

【0034】[0034]

【表1】 [Table 1]

【0035】[0035]

【発明の効果】本発明の製造方法によれば、溶媒除去が
容易で、重合度の高いポリイミド前駆体の粉粒体を容易
に製造できる。また、このポリイミド前駆体の粉粒体か
ら得られる成形体は、力学的特性に優れ、残留溶媒が少
ない。
According to the manufacturing method of the present invention, the solvent can be easily removed, and the powdery particles of the polyimide precursor having a high degree of polymerization can be easily manufactured. Further, the molded product obtained from the powdery particles of the polyimide precursor has excellent mechanical properties and a small residual solvent.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 水溶性ニトリル類中でテトラカルボン酸
二無水物およびジアミンを重合することを特徴とするポ
リイミド前駆体粉粒体の製造方法。
1. A method for producing a polyimide precursor powder, which comprises polymerizing a tetracarboxylic dianhydride and a diamine in a water-soluble nitrile.
JP20276393A 1993-07-23 1993-07-23 Production of polyimide precursor powder Pending JPH0733872A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20276393A JPH0733872A (en) 1993-07-23 1993-07-23 Production of polyimide precursor powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20276393A JPH0733872A (en) 1993-07-23 1993-07-23 Production of polyimide precursor powder

Publications (1)

Publication Number Publication Date
JPH0733872A true JPH0733872A (en) 1995-02-03

Family

ID=16462768

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20276393A Pending JPH0733872A (en) 1993-07-23 1993-07-23 Production of polyimide precursor powder

Country Status (1)

Country Link
JP (1) JPH0733872A (en)

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