JP3386383B2 - Method for producing polyimide - Google Patents

Method for producing polyimide

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Publication number
JP3386383B2
JP3386383B2 JP26152398A JP26152398A JP3386383B2 JP 3386383 B2 JP3386383 B2 JP 3386383B2 JP 26152398 A JP26152398 A JP 26152398A JP 26152398 A JP26152398 A JP 26152398A JP 3386383 B2 JP3386383 B2 JP 3386383B2
Authority
JP
Japan
Prior art keywords
polyimide
producing
solvent
reaction
phosphaphenanthrene
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
Application number
JP26152398A
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Japanese (ja)
Other versions
JP2000086761A (en
Inventor
▲あきら▼ 谷内
晋一 門野
清志 三島
桂三 塚本
勝 森
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Manac Inc
Original Assignee
Manac Inc
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Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、ポリイミドを、特
定の触媒を用いて一段法で製造する方法に関する。
TECHNICAL FIELD The present invention relates to a method for producing a polyimide by a one-step method using a specific catalyst.

【0002】[0002]

【従来の技術】ポリイミドは、加工性、電気絶縁性、機
械的強度などに優れており、耐熱性が要求される各種分
野で期待されている材料である。従来、ポリイミドは、
テトラカルボン酸無水物とジアミンを反応させ、前駆体
のポリアミック酸をつくり、これを高温で長時間、加熱
脱水、環化させる方法により製造されてきた。しかし、
ポリアミック酸は不安定で、水分で容易に加水分解し、
保存安定性が良くないという欠点があった。これまで、
ポリアミック酸からポリイミドをつくる触媒として、無
水酢酸とトリエチルアミン、ピリジンと無水酢酸、ピリ
ジンと亜リン酸トリフェニルを使用する方法が提案され
ているが、実用的な方法ではなかった。また、一段法で
ポリイミドを製造する方法では、複合触媒を使用し、1
60〜180℃の高い温度で反応させる方法が提案され
ているにすぎない。
2. Description of the Related Art Polyimide is a material expected to be used in various fields requiring heat resistance because it is excellent in workability, electrical insulation, mechanical strength and the like. Conventionally, polyimide is
It has been produced by a method in which a tetracarboxylic acid anhydride and a diamine are reacted to form a precursor polyamic acid, which is heated and dehydrated at a high temperature for a long time and cyclized. But,
Polyamic acid is unstable and easily hydrolyzes with water,
It had the drawback of poor storage stability. So far
A method using acetic anhydride and triethylamine, pyridine and acetic anhydride, or pyridine and triphenyl phosphite as catalysts for producing polyimide from polyamic acid has been proposed, but it was not a practical method. Further, in the method for producing a polyimide by the one-step method, a composite catalyst is used,
Only a method of reacting at a high temperature of 60 to 180 ° C. has been proposed.

【0003】[0003]

【発明が解決しようとする課題】本発明、上記方法を改
善し、一段階でポリイミドを製造する実用的な方法を確
立することを課題とする。
It is an object of the present invention to improve the above method and establish a practical method for producing a polyimide in one step.

【0004】[0004]

【課題を解決するための手段】本発明の方法は、テトラ
カルボン酸無水物とジアミンを、モル比1〜0.5:
0.5〜1の割合で、溶媒中、不活性ガス気流中で、触
媒として下記式Iの9,10−ジヒドロ−9−オキサ−
10−ホスファフェナンスレン−10−オキサイドの存
在下で反応させるポリイミドの製造方法である。
The method of the present invention comprises a tetracarboxylic anhydride and a diamine in a molar ratio of 1 to 0.5:
9,10-dihydro-9-oxa- of the following formula I as a catalyst in a solvent in an inert gas stream in a ratio of 0.5 to 1
It is a method for producing a polyimide, which is reacted in the presence of 10-phosphaphenanthrene-10-oxide.

【0005】[0005]

【化1】 [Chemical 1]

【0006】本発明のポリイミドの製造法の1例を反応
式で示すと次のようである。
An example of the method for producing the polyimide of the present invention is shown by the reaction formula as follows.

【0007】[0007]

【化2】 [Chemical 2]

【0008】前記触媒は、0.2〜10重量%の存在下
で、脱水閉環反応させることができる。反応温度は、1
30〜160℃で行うことができる。本発明に使用する
不活性ガスとしては、窒素ガス、アルゴンガスなどが適
当である。
The catalyst can be subjected to a dehydration ring closure reaction in the presence of 0.2 to 10% by weight. Reaction temperature is 1
It can be performed at 30 to 160 ° C. As the inert gas used in the present invention, nitrogen gas, argon gas and the like are suitable.

【0009】溶媒としては、溶解度パラメーター8.5
〜9.5の芳香族溶媒と溶解度パラメーター9.0〜1
2.1の極性溶媒を、30〜70重量%:70〜30重
量%の混合溶媒として使用して脱水反応させ、相当する
ポリイミドを生成するのに必要な水が溜出したことを確
認した後、炭素数1〜4の分岐又は直鎖のアルコール、
含水アルコールなどの貧溶媒中又は水中で、ポリイミド
を沈殿させ、濾過し、必要により再度貧溶媒で洗浄、濾
過し、80〜150℃で乾燥することにより、相当する
ポリイミドを得ることができる。溶解度パラメーター
8.5〜9.5の芳香族溶媒としては、例えばトルエ
ン、キシレン、エチルベンゼン、クロルベンゼンなどが
挙げられ、単独又は混合して使用できる。また、溶解度
パラメーター9.0〜12.1の極性溶媒としては、例
えばジメチルアセトアミド、ジエチルアセトアミド、ジ
メチルホルムアミド、ジエチルホルムアミド、イソホロ
ン、N−メチルピロリドンなどが挙げられ、単独又は混
合して使用することができる。
The solvent has a solubility parameter of 8.5.
~ 9.5 aromatic solvent and solubility parameter 9.0-1
After using the polar solvent of 2.1 as a mixed solvent of 30 to 70% by weight: 70 to 30% by weight for dehydration reaction and confirming that water necessary for producing a corresponding polyimide was distilled out. A branched or straight chain alcohol having 1 to 4 carbon atoms,
The corresponding polyimide can be obtained by precipitating the polyimide in a poor solvent such as hydrous alcohol or in water, filtering, washing again with a poor solvent if necessary, filtering, and drying at 80 to 150 ° C. Examples of the aromatic solvent having a solubility parameter of 8.5 to 9.5 include toluene, xylene, ethylbenzene, chlorobenzene, and the like, which may be used alone or in combination. Examples of the polar solvent having a solubility parameter of 9.0 to 12.1 include dimethylacetamide, diethylacetamide, dimethylformamide, diethylformamide, isophorone, N-methylpyrrolidone and the like, which may be used alone or in combination. it can.

【0010】本発明に使用するテトラカルボン酸無水物
は、炭素数4〜39の芳香族、脂環族、又は脂肪族テト
ラカルボン酸無水物であり、例えば次のものを単独で又
は2以上を混合して使用することができる。無水ピロメ
リット酸、ジフェニルエーテルテトラカルボン酸無水
物、ベンゾフェノンテトラカルボン酸無水物、マレイン
化シクロヘキセンテトラカルボン酸無水物、シクロブタ
ンテトラカルボン酸二無水物、3,3′,4,4′−ビ
フェニルテトラカルボン酸二無水物、4,4′−(1,
4−フェニレンジオキシ)フタリック無水物、2,2−
ビス(3,4−ジカルボキシフェニル)ヘキサフロロプ
ロパン二無水物、テトラリンジアンハイドライド、ペリ
レンテトラカルボキシ二無水物、1,4−ジフロロ−
2,3,5,6−ベンゼンテトラカルボン酸二無水物、
2,3,5−トリカルボキシシクロペンチル酢酸二無水
物、ビシクロ(2,2,1)ヘプタンテトラカルボン酸
二無水物、ビシクロ(2,2,2)オクト−7−エン−
2,3,5,6−テトラカルボキシリック二無水物、ブ
タンテトラカルボン酸二無水物、ジフェニルスルホンテ
トラカルボン酸二無水物。
The tetracarboxylic acid anhydride used in the present invention is an aromatic, alicyclic or aliphatic tetracarboxylic acid anhydride having 4 to 39 carbon atoms. For example, the following may be used alone or in combination of two or more. It can be mixed and used. Pyromellitic anhydride, diphenyl ether tetracarboxylic acid anhydride, benzophenone tetracarboxylic acid anhydride, maleated cyclohexene tetracarboxylic acid anhydride, cyclobutane tetracarboxylic acid dianhydride, 3,3 ′, 4,4′-biphenyl tetracarboxylic acid Dianhydride, 4,4 '-(1,
4-phenylenedioxy) phthalic anhydride, 2,2-
Bis (3,4-dicarboxyphenyl) hexafluoropropane dianhydride, tetralin dianhydride, perylene tetracarboxy dianhydride, 1,4-difluoro-
2,3,5,6-benzenetetracarboxylic dianhydride,
2,3,5-Tricarboxycyclopentylacetic acid dianhydride, bicyclo (2,2,1) heptanetetracarboxylic dianhydride, bicyclo (2,2,2) oct-7-ene-
2,3,5,6-tetracarboxylic dianhydride, butanetetracarboxylic dianhydride, diphenylsulfonetetracarboxylic dianhydride.

【0011】本発明に使用するジアミンは、炭素数4〜
39の芳香族、脂環族又は脂肪族アミンである。これら
のジアミンとしては、例えば次のものを、単独で又は2
以上を混合して使用することができる。2,2−ビス
〔4−(4−アミノフェノキシ)フェニル〕プロパン、
ジアミノジフェニルスルホン、o−トリジン、4,4′
−メチレンジアニリン、ジアミノジシクロヘキシルメタ
ン、4,4′−ジアミノジフェニルエーテル、3
(4),8(9)−ビス(アミノメチル)トリシクロ−
〔5,2,1,02 . 6〕デカン、2,4−トルエンジア
ミン、1,3−ビス(4−アミノフェノキシ)ベンゼ
ン、ビス〔4−(4−アミノフェノキシ)フェニル〕ス
ルホン、テトラデイン、4,4′−メチレン−ビス(2
−クロロアニリン)、3,3′−ジアミノベンゾフェノ
ン、ビスアミノプロピルポリジメチルシロキサン、2,
2−ビス(3−アミノ−4−ヒドロキシフェニル)ヘキ
サフロロプロパン、2,2′−ビス(トリフロロメチ
ル)−4,4′−ジアミノビフェニル、2,2′−ビス
〔4−(4−アミノフェノキシ)フェニル〕ヘキサフロ
ロプロパン、2,7−ジアミノ−9−フルオレン、1,
10−ジアミノデカン、9,9−ビス(4−アミノフェ
ニル)フルオレン。
The diamine used in the present invention has 4 to 4 carbon atoms.
39 aromatic, alicyclic or aliphatic amines. Examples of these diamines include the following alone or
The above can be mixed and used. 2,2-bis [4- (4-aminophenoxy) phenyl] propane,
Diaminodiphenyl sulfone, o-tolidine, 4,4 '
-Methylenedianiline, diaminodicyclohexylmethane, 4,4'-diaminodiphenyl ether, 3
(4), 8 (9) -bis (aminomethyl) tricyclo-
[5,2,1,0 2.6] decane, 2,4-toluenediamine, 1,3-bis (4-aminophenoxy) benzene, bis [4- (4-aminophenoxy) phenyl] sulfone, Tetoradein, 4,4'-methylene-bis (2
-Chloroaniline), 3,3'-diaminobenzophenone, bisaminopropylpolydimethylsiloxane, 2,
2-bis (3-amino-4-hydroxyphenyl) hexafluoropropane, 2,2'-bis (trifluoromethyl) -4,4'-diaminobiphenyl, 2,2'-bis [4- (4-amino Phenoxy) phenyl] hexafluoropropane, 2,7-diamino-9-fluorene, 1,
10-diaminodecane, 9,9-bis (4-aminophenyl) fluorene.

【0012】[0012]

【実施例】以下に実施例を挙げて本発明を更に詳細に説
明するが、本発明はこれらの実施例によって限定される
ものではない。 実施例1 検水管を付けた冷却コンデンサー、温度計、撹拌機、滴
下ロート、ガス吹き込み管をセットした反応フラスコ
に、2,2′−ビス〔4−(4−アミノフェノキシ)フ
ェニル〕プロパン41g、9,10−ジヒドロ−9−オ
キサ−10−ホスファフェナンスレン−10−オキサイ
ド2.5g及びキシレン260gを入れ、窒素ガスをガ
ス吹き込み管より通入して撹拌した。次にo−ジフェニ
ルエーテルテトラカルボン酸無水物31gをジメチルア
セトアミド240gに溶解したものを、10〜30℃で
滴下した。130〜150℃で3時間反応させ、生成し
た水3.62gを(計算値3.6g)検水管より除い
た。溶媒250gを回収除去した反応生成物を、メタノ
ール500g中に注下し、固形物を濾別し、メタノール
250gで洗浄した後、80〜130℃で減圧乾燥し
た。収量67.4g(収率98.5%)、固有粘度 ηi
nh(0.5g/dl DMAC30℃)0.68dl/g、分解
温度548℃(Air)。
The present invention will be described in more detail with reference to the following examples, but the present invention is not limited to these examples. Example 1 41 g of 2,2′-bis [4- (4-aminophenoxy) phenyl] propane in a reaction flask equipped with a cooling condenser equipped with a test tube, a thermometer, a stirrer, a dropping funnel, and a gas blowing tube, 2.5 g of 9,10-dihydro-9-oxa-10-phosphaphenanthrene-10-oxide and 260 g of xylene were added, and nitrogen gas was introduced through a gas blowing tube and stirred. Next, 31 g of o-diphenyl ether tetracarboxylic acid anhydride dissolved in 240 g of dimethylacetamide was added dropwise at 10 to 30 ° C. The reaction was carried out at 130 to 150 ° C. for 3 hours, and 3.62 g of water produced (calculated value 3.6 g) was removed from the test tube. The reaction product obtained by collecting and removing 250 g of the solvent was poured into 500 g of methanol, the solid matter was separated by filtration, washed with 250 g of methanol, and then dried under reduced pressure at 80 to 130 ° C. Yield 67.4 g (yield 98.5%), intrinsic viscosity ηi
nh (0.5g / dl DMAC30 ° C) 0.68dl / g, decomposition temperature 548 ° C (Air).

【0013】実施例2 実施例1と同様の装置に、4,4′−ジアミノジフェニ
ルエーテル20g及びo−キシレン120gを加えたも
のに、窒素ガスを通入し、無水ピロメリット酸21.8
gをジメチルホルムアミド100gに溶解したものを、
20〜40℃で加えた。これに9,10−ジヒドロ−9
−オキサ−10−ホスファフェナンスレン−10−オキ
サイド0.84gを加え、135〜140℃で3.5時
間反応させ、生成した水3.61g(計算量3.6g)
を検水管より除いた。反応生成物を10℃に冷却し、結
晶物を濾別した。結晶をメタノール100gで洗浄後、
135℃で熱風乾燥した。収量37.8g(収率99
%)、分解温度559℃(Air)。従来のポリアミック
酸を経由2段階法と比べると、低温(135〜148
℃)でポリイミドを得ることができた。
Example 2 A device similar to that of Example 1 except that 20 g of 4,4'-diaminodiphenyl ether and 120 g of o-xylene were added, nitrogen gas was passed through, and pyromellitic anhydride 21.8 was introduced.
g dissolved in 100 g of dimethylformamide,
Added at 20-40 ° C. With this 9,10-dihydro-9
-Oxa-10-phosphaphenanthrene-10-oxide (0.84 g) was added, and the mixture was reacted at 135 to 140 ° C for 3.5 hours to produce water (3.61 g, calculated amount: 3.6 g).
Was removed from the test tube. The reaction product was cooled to 10 ° C. and the crystalline substance was filtered off. After washing the crystals with 100 g of methanol,
It was dried with hot air at 135 ° C. Yield 37.8 g (yield 99
%), Decomposition temperature 559 ° C. (Air). Compared with the conventional two-step method using polyamic acid, the low temperature (135-148
A polyimide could be obtained at (.degree. C.).

【0014】実施例3 実施例1と同様の装置に、ジフェニルスルホンテトラカ
ルボン酸二無水物17.9g、キシレン120g及びジ
メチルアセトアミド110gを仕込み、窒素ガスを通入
し、2,2′−ビス〔4−(4−アミノフェノキシ)フ
ェニル〕プロパン20.5gを20〜40℃で分割添加
した後、9,10−ジヒドロ−9−オキサ−10−ホス
ファフェナンスレン−10−オキサイド1.15gを加
え、140〜148℃で3時間反応させ、生成水1.8
5g(計算値1.8g)を分離した。溶媒70gを留去
した後、メタノール300g中に注下した。固形物を濾
別し、再度メタノール100gで洗浄後、分離した粉末
を80℃で1時間、140℃で5時間乾燥した。収量3
5.9g(収率98%)、ηinh(0.5g/dl DMA
C 30℃)0.51dl/g、分解温度527℃(Air)。
Example 3 A device similar to that of Example 1 was charged with 17.9 g of diphenylsulfone tetracarboxylic acid dianhydride, 120 g of xylene and 110 g of dimethylacetamide, and nitrogen gas was introduced thereinto to obtain 2,2'-bis [ After 20.5 g of 4- (4-aminophenoxy) phenyl] propane was added portionwise at 20 to 40 ° C., 1.15 g of 9,10-dihydro-9-oxa-10-phosphaphenanthrene-10-oxide was added. In addition, the reaction was carried out at 140 to 148 ° C. for 3 hours to obtain 1.8
5 g (calculated value 1.8 g) was separated. After distilling off 70 g of the solvent, it was poured into 300 g of methanol. The solid matter was filtered off, washed again with 100 g of methanol, and the separated powder was dried at 80 ° C. for 1 hour and 140 ° C. for 5 hours. Yield 3
5.9 g (yield 98%), ηinh (0.5 g / dl DMA
C 30 ° C.) 0.51 dl / g, decomposition temperature 527 ° C. (Air).

【0015】実施例4 実施例1と同様の装置に、次式のジアミン19.4g及
びモノクロロベンゼン150gを入れ、窒素ガス通入
し、これにジフェニルエーテルテトラカルボン酸無水物
31gをジメチルアセトアミド120gに溶解したもの
を、20〜40℃で加えた。
Example 4 In a device similar to that of Example 1, 19.4 g of the following diamine and 150 g of monochlorobenzene were introduced, and nitrogen gas was introduced, and 31 g of diphenyl ether tetracarboxylic acid anhydride was dissolved in 120 g of dimethylacetamide. Was added at 20-40 ° C.

【0016】[0016]

【化3】 [Chemical 3]

【0017】これに9,10−ジヒドロ−9−オキサ−
10−ホスファフェナンスレン−10−オキサイド2g
を加え、140〜150℃で3.5時間反応させ、生成
した水3.63g(計算値3.6g)を除去した。反応
系から溶媒90gを留去したものを、メタノール500
g中に加え、固体を分離し、更にメタノール200gで
洗浄した固体成分を、80℃で1時間、140℃で5時
間乾燥した。収量45.4g(収率97%)、ηinh
(0.5g/dl DMAC 30℃)0.32、分解温度
477℃(Air)。
To this, 9,10-dihydro-9-oxa-
10-phosphaphenanthrene-10-oxide 2 g
Was added and the mixture was reacted at 140 to 150 ° C. for 3.5 hours to remove 3.63 g (calculated value 3.6 g) of produced water. After removing 90 g of the solvent from the reaction system, methanol 500
The solid component was separated into solids which had been washed with 200 g of methanol and dried at 80 ° C. for 1 hour and 140 ° C. for 5 hours. Yield 45.4 g (97% yield), ηinh
(0.5 g / dl DMAC 30 ° C) 0.32, decomposition temperature 477 ° C (Air).

【0018】実施例5 4,4′−ヘキサフロロイソプロピリデンジフタル酸無
水物22.2gに、キシレン100g及びジメチルホル
ムアミド80gを、実施例1と同様の装置に入れ、アル
ゴンガスを通入し、1,4−フェニレンジアミン5.5
gを30〜40℃で加えたものに、9,10−ジヒドロ
−9−オキサ−10−ホスファフェナンスレン−10−
オキサイド0.55gを加え、135〜143℃で4時
間反応させ、生成した留出水1.85g(計算値1.8
g)を除去し、溶媒80gを除いたものを20℃に冷却
し、メタノール300gを加え、析出した固形物を濾別
し、再度、メタノール100gで洗浄し、濾過した後、
140℃で5時間乾燥した。収量25g(収率97
%)、ηinh(0.5g/dl NMP 30℃)0.33、
分解温度554℃(Air)。
Example 5 To 22.2 g of 4,4'-hexafluoroisopropylidene diphthalic anhydride, 100 g of xylene and 80 g of dimethylformamide were placed in the same apparatus as in Example 1, and argon gas was introduced. 1,4-Phenylenediamine 5.5
g added at 30-40 ° C., 9,10-dihydro-9-oxa-10-phosphaphenanthrene-10-
Oxide (0.55 g) was added, and the mixture was reacted at 135 to 143 ° C. for 4 hours to generate 1.85 g of distilled water (calculated value 1.8).
g) was removed and 80 g of the solvent was removed, cooled to 20 ° C., 300 g of methanol was added, the precipitated solid was filtered off, washed again with 100 g of methanol and filtered,
It was dried at 140 ° C. for 5 hours. Yield 25g (Yield 97
%), Ηinh (0.5 g / dl NMP 30 ° C.) 0.33,
Decomposition temperature 554 ° C (Air).

【0019】実施例1と同様の装置に、2,2′−ビス
〔4−(4−アミノフェノキシ)フェニル〕プロパン1
6.4g及びキシレン120gを仕込み、窒素ガスを通
入し、20〜80℃で、o−ジフェニルエーテルテトラ
カルボン酸無水物6.2gをジメチルアセトアミド80
gに溶解したものを加えた後、9,10−ジヒドロ−9
−オキサ−10−ホスファフェナンスレン−10−オキ
サイド0.6gを加え、140〜145℃で3時間反応
させ、生成した水0.74g(計算値0.72g)を除
き、溶媒130gを留去した。反応生成物を20℃に冷
却し、メタノール200ml中に加え、結晶化したものを
濾別し、メタノール50mlで洗浄濾別し、80℃で2時
間、130℃で3時間乾燥した。収量21.1g(収率
96.4%)、アミン価102.21(計算値102.
56)。
2,2'-bis [4- (4-aminophenoxy) phenyl] propane 1 was placed in the same apparatus as in Example 1.
6.4 g and xylene 120 g were charged, nitrogen gas was introduced, and at 20 to 80 ° C., 6.2 g of o-diphenyl ether tetracarboxylic acid anhydride was added to dimethylacetamide 80.
After adding the one dissolved in g, 9,10-dihydro-9
-Oxa-10-phosphaphenanthrene-10-oxide (0.6 g) was added, and the mixture was reacted at 140 to 145 ° C for 3 hours to remove water (0.74 g) (calculated value 0.72 g). I left. The reaction product was cooled to 20 ° C., added to 200 ml of methanol, the crystallized product was filtered off, washed with 50 ml of methanol and filtered off, and dried at 80 ° C. for 2 hours and at 130 ° C. for 3 hours. Yield 21.1 g (yield 96.4%), amine value 102.21 (calculated value 102.21).
56).

───────────────────────────────────────────────────── フロントページの続き (72)発明者 塚本 桂三 広島県福山市箕沖町92番地 マナック株 式会社 箕沖工場内 (72)発明者 森 勝 広島県福山市箕沖町92番地 マナック株 式会社 箕沖工場内 (56)参考文献 特開2001−213961(JP,A)   ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Keizo Tsukamoto               92 Manooki-cho, Fukuyama-shi, Hiroshima Manac stock               Ceremony company Minohoki factory (72) Inventor Masaru Mori               92 Manooki-cho, Fukuyama-shi, Hiroshima Manac stock               Ceremony company Minohoki factory                (56) References JP 2001-213961 (JP, A)

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 テトラカルボン酸無水物とジアミンを、
モル比1〜0.5:0.5〜1の割合で、溶媒中、不活
性ガス気流中で、9,10−ジヒドロ−9−オキサ−1
0−ホスファフェナンスレン−10−オキサイドの存在
下で反応させるポリイミドの製造方法。
1. A tetracarboxylic acid anhydride and a diamine,
At a molar ratio of 1 to 0.5: 0.5 to 9,10-dihydro-9-oxa-1 in a solvent in an inert gas stream.
A method for producing a polyimide, which comprises reacting in the presence of 0-phosphaphenanthrene-10-oxide.
【請求項2】 9,10−ジヒドロ−9−オキサ−10
−ホスファフェナンスレン−10−オキサイドを、0.
2〜10重量%の存在下で反応させる、請求項1記載の
ポリイミドの製造方法。
2. 9,10-Dihydro-9-oxa-10
-Phosphaphenanthrene-10-oxide was added to 0.
The method for producing a polyimide according to claim 1, wherein the reaction is performed in the presence of 2 to 10% by weight.
【請求項3】 反応を、溶解度パラメーター8.5〜
9.5の芳香族系溶媒と溶解度パラメーター9.0〜1
2.1の極性溶媒の混合液中で行う、請求項1記載のポ
リイミドの製造方法。
3. The reaction is carried out with a solubility parameter of 8.5-
9.5 aromatic solvents and solubility parameters 9.0-1
The method for producing a polyimide according to claim 1, which is carried out in a mixed solution of the polar solvent of 2.1.
【請求項4】 反応を、130〜160℃の温度で行
う、請求項1記載のポリイミドの製造方法。
4. The method for producing a polyimide according to claim 1, wherein the reaction is performed at a temperature of 130 to 160 ° C.
【請求項5】 請求項3記載の溶媒中、9,10−ジヒ
ドロ−9−オキサ−10−ホスファフェナンスレン−1
0−オキサイドの存在下、ポリアミック酸を脱水させる
工程を含む、ポリイミドの製造方法。
5. In the solvent according to claim 3, 9,10-dihydro-9-oxa-10-phosphaphenanthrene-1.
A method for producing a polyimide, comprising a step of dehydrating a polyamic acid in the presence of 0-oxide.
JP26152398A 1998-09-16 1998-09-16 Method for producing polyimide Expired - Fee Related JP3386383B2 (en)

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