JPH0611798B2 - Manufacturing method of polyimide molding - Google Patents
Manufacturing method of polyimide moldingInfo
- Publication number
- JPH0611798B2 JPH0611798B2 JP60004102A JP410285A JPH0611798B2 JP H0611798 B2 JPH0611798 B2 JP H0611798B2 JP 60004102 A JP60004102 A JP 60004102A JP 410285 A JP410285 A JP 410285A JP H0611798 B2 JPH0611798 B2 JP H0611798B2
- Authority
- JP
- Japan
- Prior art keywords
- ring closure
- imide ring
- molding
- resin
- polyimide
- 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 - Fee Related
Links
Landscapes
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)
- Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は,成形性及び成形後の機械特性が改善されたポ
リイミド成形品の製造方法に関するものである。TECHNICAL FIELD The present invention relates to a method for producing a polyimide molded article having improved moldability and mechanical properties after molding.
(従来の技術) ポリイミド樹脂はその優れた耐熱性,機械特性等のため
に,電気・電子機器産業,自動車産業等において重要な
位置を占めており,特に近年,機器の高速化,高性能化
が進むにつれて必要不可欠な素材となりつつある。なか
でも特公昭39−22196で開示されているポリピロ
メリットイミド樹脂に代表される芳香族系のポリイミド
樹脂は極めて優れた熱安定性を有しており,いわゆる耐
熱樹脂の頂点に立っているが,反面流動性が乏しいため
成形が困難であり,成形性の改善が望まれている。(Prior Art) Polyimide resin occupies an important position in the electric / electronic device industry, the automobile industry, etc. due to its excellent heat resistance and mechanical properties. Is becoming an indispensable material as is progressing. Among them, aromatic polyimide resins typified by polypyromellitimide resin disclosed in Japanese Patent Publication No. 39-22196 have extremely excellent thermal stability and are at the top of so-called heat resistant resins. On the other hand, since the fluidity is poor, molding is difficult, and improvement in moldability is desired.
(発明が解決しようとする問題点) そこで本発明者は,ポリイミド樹脂の成形性を改善すべ
く鋭意検討した結果,従来のようにイミド閉環を完結さ
せず,閉環前のアミド酸を分子鎖中に残しておくと成形
が容易になり,かつ成形後の機械特性が向上することを
見出し,本発明に到達した。(Problems to be Solved by the Invention) Therefore, as a result of intensive studies to improve the moldability of the polyimide resin, the present inventor did not complete the imide ring closure as in the conventional case, and the amic acid before ring closure was in the molecular chain. The present invention has been completed by discovering that if left untreated, the molding becomes easier and the mechanical properties after molding are improved.
(問題点を解決するための手段) すなわち本発明は,下記一般式(I)で表わされる繰り
返し単位が主要構造単位であり,かつイミド閉環率が4
0%以上,95%以下であるアミド酸含有ポリイミド樹
脂であって,かつ粉末状樹脂を加圧成形することを特徴
とするポリイミド成形品の製造方法を提供するものであ
る。(Means for Solving Problems) That is, according to the present invention, the repeating unit represented by the following general formula (I) is a main structural unit, and the imide ring closure ratio is 4 or less.
The present invention provides a method for producing a polyimide molded article, which comprises 0% or more and 95% or less of an amic acid-containing polyimide resin and pressure-molds a powdery resin.
ここで一般式中のm,n,lは各々ゼロ又は正の整数で
あり,Arは少なくとも1つの炭素6員環を含む4価の芳
香族残基である。Arの具体例としては, などが挙げられる。又,Ar′は2価の芳香族あるいは脂
肪族残基であり,例えば などを具体的に列挙することができる。又,(I)は単
独のポリマであっても良いし,あるいは共重合体であっ
てもかまわない。 Here, m, n, and l in the general formula are each zero or a positive integer, and Ar is a tetravalent aromatic residue containing at least one carbon 6-membered ring. As a specific example of Ar, And so on. Ar 'is a divalent aromatic or aliphatic residue, such as Etc. can be specifically listed. Further, (I) may be a single polymer or a copolymer.
このようなポリイミド樹脂の合成法は公知であり,例え
ば特公昭39−22196号公報にその詳細が開示され
ているが,テトラカルボン酸誘導体(例えば2無水物)
とジアミンとを適当な溶媒中で反応させて得たポリアミ
ド酸を加熱閉環させることにより製造される。この加熱
閉環は溶液中で行うこともできるが,ポリアミド酸をい
ったん再沈し,固体状態で閉環した方が最終成形品の物
性は高い傾向がある。前述の公告公報に代表される従来
の方法ではこの加熱閉環を十分に行ない,ほぼ100%
のイミド閉環率にしていたのであるが,本発明の要点は
このイミド閉環を完全に行わせず,ある程度未閉環アミ
ド酸のままで残しておくことにある。すなわち一般式
(I)において,イミド閉環率を40%以上,95%以
下好ましくは,70%以上,90%以下に調節すると成
形が容易になり,かつ成形後の機械特性が極めて向上す
ることが見出された。ここでイミド閉環率が40%未満
であると成形時のガス発生が激しく,成形品にボイドが
生じるため好ましくなく,又,95%より大きいと成形
性向上の効果が少なく好ましくない。また,アミド酸は
あくまでポリイミド樹脂の分子鎖中に存在していなけれ
ば効果がなく,従ってポリイミド樹脂とポリアミド酸樹
脂のブレンドでは成形性を向上させることはできない。A method for synthesizing such a polyimide resin is known, and the details thereof are disclosed in, for example, Japanese Patent Publication No. 39-22196, but a tetracarboxylic acid derivative (for example, dianhydride) is disclosed.
It is manufactured by reacting a polyamic acid obtained by reacting a diamine with a diamine in a suitable solvent to cause ring closure by heating. This heat ring closure can be performed in a solution, but the physical properties of the final molded product tend to be higher if the polyamic acid is once reprecipitated and then closed in the solid state. In the conventional method represented by the above-mentioned official gazette, this heating ring closure is sufficiently performed, and almost 100% is achieved.
Although the imide ring-closing rate was set to the above, the point of the present invention is not to completely perform the imide ring-closing but to leave the unclosed amic acid as it is to some extent. That is, in the general formula (I), when the imide ring closure rate is adjusted to 40% or more and 95% or less, preferably 70% or more and 90% or less, the molding becomes easy and the mechanical properties after the molding are significantly improved. Was found. Here, if the imide ring closure rate is less than 40%, gas generation during molding is intense and voids are generated in the molded product, which is not preferable, and if it exceeds 95%, the effect of improving the moldability is small, which is not preferable. Further, the amic acid has no effect unless it is present in the molecular chain of the polyimide resin, and therefore the blendability of the polyimide resin and the polyamic acid resin cannot improve the moldability.
本発明でいうところのイミド閉環率はいくつかの手法に
より定量化することが可能であるが,赤外吸収スペクト
ルを用いるのが最も簡便である。すなわち一般式(I)
で示すような構造を持つイミド基は,600cm-1に特性
吸収を有しているため,ベンゼン環の振動に基づく89
0cm-1の吸収を標準とし,両者の吸光度比aをイミド閉
環率の指標とする。次にイミド閉環が100%完結した
と見なされる試料についてaを測定し,次式によりイミ
ド閉環率を求める。後で述べる実施例においては,イミ
ド閉環率100%の試料として,400℃で熱処理した
ものを用いた。The imide ring closure rate as referred to in the present invention can be quantified by several methods, but the infrared absorption spectrum is the most convenient. That is, the general formula (I)
The imide group having the structure as shown in Figure 6 has a characteristic absorption at 600 cm -1 , so it is based on the vibration of the benzene ring.
The absorption at 0 cm -1 is used as a standard, and the absorbance ratio a of both is used as an index of the imide ring closure rate. Next, a is measured for a sample which is considered to be 100% complete with imide ring closure, and the imide ring closure rate is determined by the following formula. In the examples described later, a sample heat-treated at 400 ° C. was used as a sample having an imide ring closure rate of 100%.
本発明では,イミド閉環率40%以上,95%以下,好
ましくは70%以上90%以下のポリイミド樹脂を加圧
成形することを特徴とするが,このイミド閉環率の調節
は具体的には,閉環時の加熱温度を上下させることによ
り行われる。そして好ましいイミド閉環率を有した樹脂
を調整するには,閉環温度は150℃から200℃の範
囲が好ましい。又,この加熱温度が300℃以上になる
とイミド閉環率はほぼ100%に近くなり,成形時の流
動性が明らかに低下してくる。 The present invention is characterized in that a polyimide resin having an imide ring closure rate of 40% or more and 95% or less, preferably 70% or more and 90% or less is pressure-molded. It is performed by raising or lowering the heating temperature at the time of ring closure. Then, in order to adjust the resin having a preferable imide ring closure rate, the ring closure temperature is preferably in the range of 150 ° C to 200 ° C. Further, when the heating temperature is 300 ° C. or higher, the imide ring closure rate becomes close to 100%, and the fluidity during molding obviously decreases.
本発明で対象とするポリイミド樹脂は,一般に溶融流動
性に乏しい。従って本発明による手法が有効になるので
あるが,同時に樹脂の形態及び成形圧力の2点も,成形
品の特性を左右する重要な因子である。すなわち樹脂は
微粉末状に粉砕されていなければならない。また成形圧
力は好ましくは少なくとも500kgf/cm2であり,更に好ま
しくは1.5×103kgf/cm2以上である。The polyimide resin targeted by the present invention generally has poor melt fluidity. Therefore, the method according to the present invention is effective, but at the same time, two points of the form of the resin and the molding pressure are important factors that influence the characteristics of the molded product. That is, the resin must be ground into a fine powder. The molding pressure is preferably at least 500 kgf / cm 2 , and more preferably 1.5 × 10 3 kgf / cm 2 or more.
本発明でいう加圧成形とは,金型中で樹脂を圧縮し,望
ましい形状の成形品にすることを示すが通常は同時に金
型を加熱する。しかし室温で成形した後,圧力をかけず
に加熱のみにより最終製品にすることもでき,これは一
般に焼結成形と呼ばれる。又,焼結成形品を更に加熱圧
縮し,物性の向上を計る場合もある。The term “pressure molding” as used in the present invention means that a resin is compressed in a mold to obtain a molded product having a desired shape, but the mold is usually heated at the same time. However, after molding at room temperature, it is also possible to make the final product only by heating without applying pressure, which is generally called sinter molding. Further, the sintered molded product may be further heated and compressed to improve the physical properties.
本発明のポリイミド成形品には必要に応じて種々の添加
剤を配合し,望ましい特性を付与することもできるが,
そのような添加剤の例としては,フッ素樹脂,グラファ
イト,二硫化モリブデン,マイカ,タルク,ガラス繊
維,カーボン繊維,アルミニウム,銀,各種金属酸化物
等が挙げられる。これらの添加剤は重合の過程で既に配
合しておくこともできるし,又成形前に配合することも
できるが,いずれにしても均一に分散させることが望ま
しい。Although various additives may be added to the polyimide molded article of the present invention as needed to impart desired properties,
Examples of such additives include fluororesins, graphite, molybdenum disulfide, mica, talc, glass fibers, carbon fibers, aluminum, silver and various metal oxides. These additives may be blended in the course of polymerization or may be blended before molding, but in any case, it is desirable to uniformly disperse them.
以下に実施例を挙げて本発明をさらに詳述する。なお,
実施例において樹脂の粉砕は,ホソカワミクロン(株)
のバンタムミルを用いた。又,加圧成形は次の様な方法
で行った。すなわち,金型中に樹脂を充填し,室温にお
いて3×103kgf/cm2の圧力をかける。次にこれを徐々に
昇温し,最終的に450℃まで加熱する。この昇温過程
で残存アミド酸の脱水に伴うガスが発生するため,時々
放圧しガスを抜くようにする。450℃で5分間保った
後,加圧したまま冷却し,300℃以下になったところ
で取り出す。次にこの成形品から,65mm×13mm×3
mmの試験片を切り出し,引張及び曲げ試験に供した。Hereinafter, the present invention will be described in more detail with reference to examples. In addition,
In the examples, the resin is crushed by Hosokawa Micron Co., Ltd.
Bantam mill was used. The pressure molding was performed by the following method. That is, the mold is filled with resin and a pressure of 3 × 10 3 kgf / cm 2 is applied at room temperature. Next, this is gradually heated and finally heated to 450 ° C. During this temperature raising process, gas is generated due to dehydration of residual amic acid, so pressure is released from time to time to release the gas. After keeping at 450 ° C for 5 minutes, it is cooled while being pressurized, and taken out when it becomes 300 ° C or less. Next, from this molded product, 65 mm × 13 mm × 3
mm test pieces were cut out and subjected to tensile and bending tests.
実施例1 4,4′−ジアミノジフエニルエーテル(DDE)60.
07g(0.3mol)を1.2のN,N−ジメチルアセト
アミド(DMAc)に溶解し,これにピロメリット酸2無水
物(PMDA)65.44g(0.3mol)を徐々に加え
た。添加終了後,さらに1時間攪拌を続けたところ,η
inh(DMAc中に,濃度0.5g/d,30℃で測定)が2.
24のポリアミド酸溶液が得られた。次にこれをトルエ
ン10,無水酢酸0.5,ピリジン0.5よりな
る混合溶媒中に激しく攪拌しながら徐々に添加し,生じ
た沈澱を過した。これをアセトンで2回洗浄後,熱風
乾燥機中100℃で8時間乾燥し,さらに粉砕した後,
真空乾燥機中170℃で5時間熱処理した。得られたポ
リイミド樹脂粉末のイミド閉環率を赤外吸収スペクトル
により測定したところ,77%であった。続いてこの粉
末を加圧成形し,引張および曲げ試験を行った。結果を
表1に示したが,後で述べる比較例のように100%イ
ミド閉環させたものに比べ,優れた特性を有していた。
すなわち,未閉環アミド酸を残しておくと,成形時の流
動性,合着性が良くなり,成形品の機械特性が向上する
ことがわかった。Example 1 4,4'-Diaminodiphenyl ether (DDE) 60.
07 g (0.3 mol) was dissolved in 1.2 N, N-dimethylacetamide (DMAc), and pyromellitic dianhydride (PMDA) 65.44 g (0.3 mol) was gradually added thereto. When the stirring was continued for another hour after the addition was completed,
inh (measured in DMAc at a concentration of 0.5 g / d at 30 ° C.) is 2.
24 polyamic acid solutions were obtained. Next, this was gradually added to a mixed solvent consisting of toluene 10, 0.5 acetic anhydride and 0.5 pyridine with vigorous stirring, and the resulting precipitate was passed. This was washed twice with acetone, dried in a hot air dryer at 100 ° C for 8 hours, and further pulverized,
Heat treatment was performed at 170 ° C. for 5 hours in a vacuum dryer. The imide ring closure rate of the obtained polyimide resin powder was 77% when measured by infrared absorption spectrum. Subsequently, this powder was pressed and subjected to tensile and bending tests. The results are shown in Table 1, and had excellent properties as compared with those obtained by 100% imide ring closure as in Comparative Examples described later.
That is, it was found that leaving unclosed amic acid improves the fluidity and coalescence during molding, and improves the mechanical properties of the molded product.
実施例2 DDE 60.07g(0.3mol)を1.2のDMAcに溶
解し、これにPMDA32.72g(0.15mol)およびベンゾフエ
ノンテトラカルボン酸2無水物(BTDA)48.33
g(0.15mol)を徐々に加えた。添加終了後さらに1時
間攪拌を続けたところ,ηinh(DMAc中,濃度0.5g/d
,30℃で測定)が1.82のポリアミド酸溶液が得
られた。実施例1と同様な方法により,再沈,乾燥,粉
砕した後,真空乾燥機中,200℃で5時間熱処理し
た。得られた共重合ポリイミド樹脂粉末のイミド閉環率
を赤外吸収スペクトルにより測定したところ85%であ
った。続いてこの粉末を加圧成形し,引張および曲げ試
験を行った。結果を表2に示したが,100%イミド閉
環させたものに比べ優れていた。Example 2 DDE 60.07 g (0.3 mol) was dissolved in 1.2 DMAc, PMDA 32.72 g (0.15 mol) and benzophenone tetracarboxylic dianhydride (BTDA) 48.33 were dissolved in this.
g (0.15 mol) was added slowly. When stirring was continued for an additional 1 hour after the addition was completed, η inh (in DMAc, concentration 0.5 g / d
, Measured at 30 ° C.) was 1.82 to obtain a polyamic acid solution. After reprecipitation, drying, and pulverization in the same manner as in Example 1, heat treatment was performed in a vacuum dryer at 200 ° C. for 5 hours. The imide ring closure rate of the obtained copolymerized polyimide resin powder was measured by infrared absorption spectrum and found to be 85%. Subsequently, this powder was pressed and subjected to tensile and bending tests. The results are shown in Table 2 and were superior to those obtained by 100% imide ring closure.
比較例1 実施例1において,真空乾燥機による加熱処理を330
℃で行ったところ,イミド閉環率約100%のポリイミ
ド樹脂粉末が得られた。これを用いた加圧成形品の引張
および曲げ試験結果を表1に示したが,実施例のように
アミド酸を残したものに比べて劣っていた。Comparative Example 1 In Example 1, the heat treatment by the vacuum dryer was 330
When it was carried out at 0 ° C., a polyimide resin powder having an imide ring closure rate of about 100% was obtained. The results of tensile and bending tests of the pressure-molded product using this are shown in Table 1, but they were inferior to those of the example in which the amic acid was left as in the example.
比較例2 実施例2において,真空乾燥機による加熱処理を330
℃で行ったところ,得られたポリイミド樹脂粉末のイミ
ド閉環率は約100%であった。表2にこれを用いた加
圧成形品の引張および曲げ試験結果を示したが,実施例
に比べて劣っていた。Comparative Example 2 In Example 2, the heat treatment by the vacuum dryer was 330
When it was carried out at 0 ° C., the polyimide resin powder obtained had an imide ring closure rate of about 100%. Table 2 shows the results of tensile and bending tests of pressure-molded products using the same, but they were inferior to the examples.
(発明の効果) 実施例及び比較例より明らかなように,本発明による手
法を用いると,本来成形困難なポリイミド樹脂の成形性
が向上し,その結果として成形品の機械特性が向上す
る。これはアミド酸が残存しているため,加圧時に分子
が動きやすくなり,粉末間の合着性が増したためと考え
られる。こうして得られたポリイミド成形品は優れた耐
熱性,機械特性,摺動特性等を有しており,電気・電子
機器部品,自動車部品,事務機部品、航空機部品等に有
用である。(Effects of the Invention) As is clear from the examples and comparative examples, when the method according to the present invention is used, the moldability of a polyimide resin that is originally difficult to mold is improved, and as a result, the mechanical properties of the molded product are improved. It is considered that this is because the amic acid remained, so that the molecules moved easily during pressurization and the cohesiveness between the powders increased. The polyimide molded product thus obtained has excellent heat resistance, mechanical properties, sliding properties, etc., and is useful for electric / electronic device parts, automobile parts, office machine parts, aircraft parts, and the like.
Claims (1)
位が主要構造単位であり,かつイミド閉環率が40%以
上,95%以下であるアミド酸含有ポリイミド樹脂であ
って,かつ粉末状樹脂を加圧成形することを特徴とする
ポリイミド成形品の製造方法。 (式中m,n,lは各々ゼロ又は正の整数,Arは少なく
とも一つの炭素6員環を含む4価の芳香族残基,Ar′は
2価の芳香族あるいは脂肪族残基を示す。)1. A amide acid-containing polyimide resin in which a repeating unit represented by the following general formula (I) is a main structural unit, and an imide ring closure rate is 40% or more and 95% or less, and a powdery resin. A method for producing a polyimide molded article, which comprises press molding. (Where m, n and l are each a zero or positive integer, Ar is a tetravalent aromatic residue containing at least one carbon 6-membered ring, Ar 'is a divalent aromatic or aliphatic residue. .)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60004102A JPH0611798B2 (en) | 1985-01-16 | 1985-01-16 | Manufacturing method of polyimide molding |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60004102A JPH0611798B2 (en) | 1985-01-16 | 1985-01-16 | Manufacturing method of polyimide molding |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61163937A JPS61163937A (en) | 1986-07-24 |
| JPH0611798B2 true JPH0611798B2 (en) | 1994-02-16 |
Family
ID=11575423
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60004102A Expired - Fee Related JPH0611798B2 (en) | 1985-01-16 | 1985-01-16 | Manufacturing method of polyimide molding |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0611798B2 (en) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2590213B2 (en) * | 1988-07-06 | 1997-03-12 | 東レ株式会社 | Spherical polyimide powder |
| US4943682A (en) * | 1988-12-15 | 1990-07-24 | Ethyl Corporation | Production of particulate polyimide polymers |
| JP2564028B2 (en) * | 1990-08-24 | 1996-12-18 | 鐘淵化学工業株式会社 | Polyimide resin powder and molded body |
| JPH04142332A (en) * | 1990-10-03 | 1992-05-15 | Kanegafuchi Chem Ind Co Ltd | Production of polyimide resin powder |
| US5898048A (en) * | 1996-04-05 | 1999-04-27 | Ube Industries, Ltd. | Polyimide powder and process for producing powder molded body |
| KR100351627B1 (en) * | 2000-01-04 | 2002-09-11 | 한국화학연구원 | Colorless polyimides with good adhesion and their hybrids |
| KR100366147B1 (en) * | 2000-02-01 | 2003-01-14 | 한국화학연구원 | Polyimide nanocomposite powder with high crystallinity and a method for preparing the same |
| KR20240102471A (en) * | 2022-12-26 | 2024-07-03 | 피아이첨단소재 주식회사 | Polyimide molded product and manufacturing method same |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1132964A (en) * | 1964-11-25 | 1968-11-06 | Ici Ltd | Moulding of polymeric materials |
| US3842026A (en) * | 1970-04-17 | 1974-10-15 | Ici Ltd | Aromatic part-cured polyimidene moulding powders |
-
1985
- 1985-01-16 JP JP60004102A patent/JPH0611798B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61163937A (en) | 1986-07-24 |
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