JPH069556A - Production of maleimide - Google Patents

Production of maleimide

Info

Publication number
JPH069556A
JPH069556A JP4167645A JP16764592A JPH069556A JP H069556 A JPH069556 A JP H069556A JP 4167645 A JP4167645 A JP 4167645A JP 16764592 A JP16764592 A JP 16764592A JP H069556 A JPH069556 A JP H069556A
Authority
JP
Japan
Prior art keywords
solvent
acid
reaction
maleimide
acid catalyst
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
JP4167645A
Other languages
Japanese (ja)
Inventor
Kaoru Kanayama
薫 金山
Yoshinobu Onuma
吉信 大沼
Hiromi Chiba
裕美 千葉
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.)
Mitsubishi Petrochemical Co Ltd
Original Assignee
Mitsubishi Petrochemical Co 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 Mitsubishi Petrochemical Co Ltd filed Critical Mitsubishi Petrochemical Co Ltd
Priority to JP4167645A priority Critical patent/JPH069556A/en
Publication of JPH069556A publication Critical patent/JPH069556A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Abstract

PURPOSE:To provide the method for simply producing the highly pure maleimide reduced in the content of ring-unclosed maleamic acid, facilitating the removal of an acid catalyst, etc., and not exhausting a halogen when a waste solvent is burnt. CONSTITUTION:The method for producing the maleimide is characterized by reacting an amine compound with maleic anhydride in the solvent mixture of an ester solvent with an aprotic polar solvent and subsequently subjecting the resultant maleamic acid to a dehydrative ring-closing reaction in the presence of an acid catalyst.

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、マレイミドの製造方法
に関する。本発明の方法で得られるマレイミドは積層材
料、封止材料、電気絶縁材料、導電性ペースト、接着剤
および構造材料として有用なものである。
FIELD OF THE INVENTION The present invention relates to a method for producing maleimide. The maleimide obtained by the method of the present invention is useful as a laminate material, a sealing material, an electric insulating material, a conductive paste, an adhesive and a structural material.

【0002】[0002]

【従来の技術】従来、マレイミドの製造方法としては、
例えば特公昭59−52660号、特開昭63−661
64号公報には、アセトン等のケトン溶媒またはN,N
−ジメチルホルムアミド等の極性溶媒の存在下、無水酢
酸等の脱水剤を用い、トリエチルアミン等の塩基及び金
属化合物を加えて脱水閉環反応する方法が、又、特開昭
60−260623、63−301226号公報には、
ポリアミンと無水マレイン酸とを芳香族炭化水素または
ハロゲン化炭化水素と非プロトン性極性溶媒との混合溶
媒中で反応させてポリアミド酸を得た後、脱水閉環反応
させる方法が開示されている。
2. Description of the Related Art Conventionally, as a method for producing maleimide,
For example, JP-B-59-52660 and JP-A-63-661.
No. 64 discloses a ketone solvent such as acetone or N, N.
-A method of dehydration ring closure reaction by adding a base such as triethylamine and a metal compound using a dehydrating agent such as acetic anhydride in the presence of a polar solvent such as dimethylformamide, and JP-A-60-260623, 63-301226. In the gazette,
A method is disclosed in which a polyamine and maleic anhydride are reacted in a mixed solvent of an aromatic hydrocarbon or a halogenated hydrocarbon and an aprotic polar solvent to obtain a polyamic acid, and then a dehydration ring-closing reaction is performed.

【0003】[0003]

【発明が解決しようとする課題】しかし、前記の脱水剤
を用いる方法では閉環反応が十分進行せず製造されたビ
スマレイミドは未閉環のマレアミド酸がかなり存在す
る。更に、無水酢酸を脱水剤として用いる製造方法で
は、無水酢酸の使用量が多く製造コストが高い、反応に
より副生する酢酸を除去する煩雑な工程が必要である等
の問題を有する。又、触媒に金属を使用した場合、混入
防止や無害化の処置が必要となる等の種々の難点があ
る。
However, the above-mentioned method using a dehydrating agent does not allow the ring-closing reaction to proceed sufficiently, and the bismaleimide produced contains a considerable amount of unringed maleamic acid. Furthermore, the production method using acetic anhydride as a dehydrating agent has problems that the amount of acetic anhydride used is large, the production cost is high, and a complicated step of removing acetic acid by-produced by the reaction is required. Further, when a metal is used for the catalyst, there are various problems such as prevention of mixing and detoxification treatment are required.

【0004】更に、芳香族炭化水素と非プロトン性極性
溶媒との混合溶媒中で脱水閉環させる方法では、酸触媒
等を除去するための水洗工程時、マレイミド類が芳香族
炭化水素溶媒に対して溶解性が劣り、析出しやすいた
め、水洗が困難になるという問題がある。また、ハロゲ
ン化炭化水素を使用する方法では、廃溶媒の焼却時、ハ
ロゲン化水素を排出するため、環境衛生上好ましくな
い。
Further, in the method of dehydration ring closure in a mixed solvent of an aromatic hydrocarbon and an aprotic polar solvent, the maleimides react with the aromatic hydrocarbon solvent during the water washing step for removing the acid catalyst and the like. There is a problem that it is difficult to wash with water because of poor solubility and easy precipitation. In addition, the method using a halogenated hydrocarbon is not preferable in terms of environmental hygiene because the halogenated hydrocarbon is discharged when the waste solvent is incinerated.

【0005】[0005]

【課題を解決するための手段】本発明は、アミン類と無
水マレイン酸とを、エステル溶媒と非プロトン性極性溶
媒中で反応させてマレアミド酸を得、該マレアミド酸
を、酸触媒の存在下、脱水閉環反応させることを特徴と
する、純度の高いマレイミドを簡易に製造する方法を提
供するものである。
In the present invention, amines and maleic anhydride are reacted in an ester solvent and an aprotic polar solvent to obtain maleamic acid, which is then reacted in the presence of an acid catalyst. The present invention provides a method for easily producing highly pure maleimide, characterized by performing a dehydration ring closure reaction.

【0006】(アミン類)本発明に用いられるアミン類
としては、例えば、 (1)アニリン、トルイジン、クロロアニリン、ブロモ
アニリン等の芳香族モノアミン、シクロヘキシルアミン
等の脂環式モノアミン類、トリメチレンジアミン、テト
ラメチレンジアミン、ヘキサメチレンジアミン、キシリ
レンジアミン、3,9−ビス(3−アミノプロピル)−
2,4,8,10−テトラオキサスピロ〔5,5〕ウン
デカン、ビス(4−アミノシクロヘキシル)メタン等の
脂肪族ジアミン、m−フェニレンジアミン、p−フェニ
レンジアミン、4,4′−ジアミノジフェニルメタン、
4,4′−ジアミノジフェニルスルホン、4,4′−ジ
アミノジフェニルエーテル、4,4′−ジアミノジフェ
ニルスルフイド、3,3′−ジアミノジフェニルスルホ
ン、2,2−ビス−(4−アミノフェニル)プロパン、
ビス−(4−アミノフェニル)ジフェニルシラン、ビス
−(4−アミノフェニル)メチルホスフィンオキサイ
ド、ビス−(3−アミノフェニル)メチルホスフィンオ
キサイド、ビス−(4−アミノフェニル)−フェニルホ
スフィンオキサイド、ビス−(4−アミノフェニル)フ
ェニラミン、1,5ジアミノナフタレン、2,4−ジア
ミノトルエン、2,6−ジアミノトルエン、3,3′−
ジメチル−4,4′−ジアミノフェニルメタン、3,
3′−ジエチル−5,5′−ジメチル−4,4′−ジア
ミノフェニルメタン、3,3′・5,5′−テトラエチ
ル−4,4′−ジアミノジフェニルメタン、3,3′−
ジエチル−4,4′−ジアミノジフェニルメタン、3,
3′・5,5′−テトラメチル−4,4′−ジアミノジ
フェニルメタン、3,3′−ジ−n−ブチル−4,4′
−ジアミノジフェニルメタン、3,3′−ジ−tert
−ブチル−4,4′−ジアミノジフェニルメタン、2,
2−ビス−〔4−(4−アミノフェノキシ)フェニル〕
プロパン、ビス〔4−(4−アミノフェノキシ)フェニ
ル〕スルホン、ビス(3−クロロ−4−アミノフェニ
ル)メタン等の芳香族ジアミン。
(Amines) Examples of amines used in the present invention include (1) aromatic monoamines such as aniline, toluidine, chloroaniline and bromoaniline; alicyclic monoamines such as cyclohexylamine; and trimethylenediamine. , Tetramethylenediamine, hexamethylenediamine, xylylenediamine, 3,9-bis (3-aminopropyl)-
Aliphatic diamines such as 2,4,8,10-tetraoxaspiro [5,5] undecane, bis (4-aminocyclohexyl) methane, m-phenylenediamine, p-phenylenediamine, 4,4′-diaminodiphenylmethane,
4,4'-diaminodiphenyl sulfone, 4,4'-diaminodiphenyl ether, 4,4'-diaminodiphenyl sulfide, 3,3'-diaminodiphenyl sulfone, 2,2-bis- (4-aminophenyl) propane ,
Bis- (4-aminophenyl) diphenylsilane, bis- (4-aminophenyl) methylphosphine oxide, bis- (3-aminophenyl) methylphosphine oxide, bis- (4-aminophenyl) -phenylphosphine oxide, bis- (4-Aminophenyl) phenylamine, 1,5 diaminonaphthalene, 2,4-diaminotoluene, 2,6-diaminotoluene, 3,3'-
Dimethyl-4,4'-diaminophenylmethane, 3,
3'-diethyl-5,5'-dimethyl-4,4'-diaminophenylmethane, 3,3'.5,5'-tetraethyl-4,4'-diaminodiphenylmethane, 3,3'-
Diethyl-4,4'-diaminodiphenylmethane, 3,
3'.5,5'-tetramethyl-4,4'-diaminodiphenylmethane, 3,3'-di-n-butyl-4,4 '
-Diaminodiphenylmethane, 3,3'-di-tert
-Butyl-4,4'-diaminodiphenylmethane, 2,
2-bis- [4- (4-aminophenoxy) phenyl]
Aromatic diamines such as propane, bis [4- (4-aminophenoxy) phenyl] sulfone, and bis (3-chloro-4-aminophenyl) methane.

【0007】(2)アニリンとホルムアルデヒドとの縮
合反応により得られる芳香族ポリアミン(特開昭50−
21098号公報参照)。 (3)芳香族ジアルデヒドと芳香族アミンとの反応生成
物である4官能の芳香族ポリアミン(特開昭59−12
931号公報参照)。 (4)芳香族ジアルデヒドとホルムアルデヒドの混合物
と芳香族アミンとから得られる芳香族ポリアミン(特開
昭60−26032号公報参照)。 (5)その他、ビニルアニリン類の重合体、トリアミノ
ベンゼン、トリアミノトルエン、トリアミノナフタレ
ン、トリアミノジフェニル、トリアミノピリジン、トリ
アミノフェニルエーテル、トリアミノジフェニルメタ
ン、トリアミノジフェニルスルホン、トリアミノベンゾ
フェノン、トリアミノフェニルオルソホスフェート、ト
リ(アミノフェニル)ホスフィンオキサイド、テトラア
ミノベンゾフェノン、テトラアミノベンゼン、テトラア
ミノナフタレン、ジアミノベンジジン、テトラアミノフ
ェニルエーテル、テトラアミノフェニルメタン、テトラ
アミノフェニルスルホン、ビス(ジアミノフェニル)ピ
リジン、メラミン等。 が挙げられる。
(2) Aromatic polyamine obtained by condensation reaction of aniline and formaldehyde (JP-A-50-
No. 21098). (3) A tetrafunctional aromatic polyamine which is a reaction product of an aromatic dialdehyde and an aromatic amine (JP-A-59-12).
931). (4) An aromatic polyamine obtained from a mixture of aromatic dialdehyde and formaldehyde and an aromatic amine (see JP-A-60-26032). (5) Other polymers of vinylaniline, triaminobenzene, triaminotoluene, triaminonaphthalene, triaminodiphenyl, triaminopyridine, triaminophenyl ether, triaminodiphenylmethane, triaminodiphenyl sulfone, triaminobenzophenone, Triaminophenyl orthophosphate, tri (aminophenyl) phosphine oxide, tetraaminobenzophenone, tetraaminobenzene, tetraaminonaphthalene, diaminobenzidine, tetraaminophenyl ether, tetraaminophenylmethane, tetraaminophenyl sulfone, bis (diaminophenyl) pyridine , Melamine etc. Is mentioned.

【0008】(反応溶媒)本発明の方法に於て、反応溶
媒として、エステル溶媒と非プロトン性極性溶媒の混合
溶媒が用いられる。エステル溶媒としては、具体的に
は、ギ酸エチル、ギ酸n−ブチル、酢酸エチル、酢酸プ
ロピル、酢酸n−ブチル、酢酸イソブチル、酢酸sec
−ヘキシル、酢酸2−エチルヘキシル、プロピオン酸エ
チル、プロピオン酸n−ブチル、イソ吉草酸エチル等の
脂肪族エステル、マレイン酸ジメチル等の脂肪族ジエス
テル、安息香酸メチル等の芳香族エステル、γ−ブチロ
ラクトン等の環状エステル、およびカルビトールアセテ
ート等のエーテルエステル等が挙げられる。これらのう
ちで、一般式、R1 COOR2 〔式中、R1 は水素原子
または炭素数1〜8のアルキル基を示し、R2 は炭素数
1〜10のアルキル基を示す〕で表わされる脂肪族エス
テルが好ましい。
(Reaction Solvent) In the method of the present invention, a mixed solvent of an ester solvent and an aprotic polar solvent is used as a reaction solvent. Specific examples of the ester solvent include ethyl formate, n-butyl formate, ethyl acetate, propyl acetate, n-butyl acetate, isobutyl acetate, sec acetate.
-Hexyl, 2-ethylhexyl acetate, ethyl propionate, n-butyl propionate, ethyl isovalerate and other aliphatic esters, dimethyl maleate and other aliphatic diesters, methyl benzoate and other aromatic esters, γ-butyrolactone, etc. And cyclic ester of carbitol acetate and the like. Of these, represented by the general formula, R 1 COOR 2 [wherein R 1 represents a hydrogen atom or an alkyl group having 1 to 8 carbon atoms, and R 2 represents an alkyl group having 1 to 10 carbon atoms]. Aliphatic esters are preferred.

【0009】非プロトン性極性溶媒としては、アミド酸
を溶解しやすい溶媒、例えば、N,N−ジメチルホルム
アミド、N,N−ジメチルアセトアミド、N−メチル−
2−ピロリドン、1,3−ジメチル−2−イミダゾリジ
ノン、テトラメチル尿素等のアミド系溶媒、ジメチルス
ルホキシド等のイオウ系溶媒、ヘキサメチルホスホロア
ミド等のリン系溶媒、等が挙げられ、アミド系溶媒が好
ましく用いられる。これらの非プロトン性極性溶媒は、
沸点150℃以上で、水と共沸しにくいものが好まし
い。
As the aprotic polar solvent, a solvent which easily dissolves amic acid, for example, N, N-dimethylformamide, N, N-dimethylacetamide, N-methyl-
2-pyrrolidone, 1,3-dimethyl-2-imidazolidinone, amide solvents such as tetramethylurea, sulfur solvents such as dimethylsulfoxide, phosphorus solvents such as hexamethylphosphoramide, and the like, and amides. A system solvent is preferably used. These aprotic polar solvents are
A substance having a boiling point of 150 ° C. or higher and hardly azeotropic with water is preferable.

【0010】混合溶媒中のエステル溶媒と非プロトン性
極性溶媒の量は、非プロトン性極性溶媒が少ないほうが
よく、混合溶媒中の非プロトン性極性溶媒の量が、0.
1〜30重量%、好ましくは1〜20重量%である。反
応溶媒は、アミン類1重量部に対し、1〜50重量部、
好ましくは2〜20重量部の割合で使用する。
The amounts of the ester solvent and the aprotic polar solvent in the mixed solvent are preferably such that the amount of the aprotic polar solvent is small, and the amount of the aprotic polar solvent in the mixed solvent is 0.
It is 1 to 30% by weight, preferably 1 to 20% by weight. The reaction solvent is 1 to 50 parts by weight with respect to 1 part by weight of amines,
It is preferably used in a proportion of 2 to 20 parts by weight.

【0011】(酸触媒)脱水閉環反応に使用される酸触
媒としては、硫酸、無水硫酸、リン酸、ポリリン酸、メ
タリン酸、縮合リン酸等の無機酸触媒、及び、p−トル
エンスルホン酸、トリクロル酢酸、トリフルオロ酢酸、
トリフルオロメタンスルホン酸等の有機酸触媒が挙げら
れ、有機酸触媒が好ましく用いられる。これら酸触媒の
使用量は、アミン類のアミノ基1当量に対し、0.00
01〜1モル、好ましくは0.001〜0.5モルの範
囲である。
(Acid catalyst) As the acid catalyst used in the dehydration ring-closing reaction, inorganic acid catalysts such as sulfuric acid, sulfuric anhydride, phosphoric acid, polyphosphoric acid, metaphosphoric acid and condensed phosphoric acid, and p-toluenesulfonic acid, Trichloroacetic acid, trifluoroacetic acid,
Examples thereof include organic acid catalysts such as trifluoromethanesulfonic acid, and organic acid catalysts are preferably used. The amount of these acid catalysts used is 0.00 with respect to 1 equivalent of amino groups of amines.
It is in the range of 01 to 1 mol, preferably 0.001 to 0.5 mol.

【0012】(反応方法)マレイミドの製造は、アミン
類のアミノ基1当量に対し、無水マレイン酸を0.9〜
2モル、好ましくは1.0〜1.3モルの範囲で前記有
機溶媒中で、0〜130℃の温度範囲で付加反応させ
て、マレアミド酸を生成させる(第1段)。第1段反応
後、該マレアミド酸を単離することなしに、反応系に所
定量の酸触媒を添加し、昇温して生成水を反応溶媒と共
沸留去しながら脱水閉環反応させて、マレイミドを得る
(第2段)。
(Reaction Method) Maleimide is prepared by adding maleic anhydride to 0.9 to 1 equivalent of amino group of amines.
Addition reaction is carried out in the temperature range of 0 to 130 ° C. in the organic solvent in an amount of 2 mol, preferably 1.0 to 1.3 mol to produce maleamic acid (first step). After the first-stage reaction, without isolating the maleamic acid, a predetermined amount of an acid catalyst was added to the reaction system, and the temperature was raised to carry out a dehydration ring-closing reaction while azeotropically distilling generated water with a reaction solvent. , Maleimide is obtained (second stage).

【0013】脱水閉環反応は、50〜200℃、好まし
くは、80〜160℃の温度範囲で生成水を共沸留去し
て脱水閉環反応をさせマレイミドとする。反応温度が5
0℃未満では、脱水反応が進行しにくく、また、200
℃を越えると重合物の生成量が多くなる。生成水と共沸
した有機溶媒は、直ちに、冷却、相分離し、再度、反応
系内に戻され反応を遂行する。
In the dehydration ring-closing reaction, the produced water is azeotropically distilled off in the temperature range of 50 to 200 ° C., preferably 80 to 160 ° C. to perform the dehydration ring-closing reaction to obtain maleimide. Reaction temperature is 5
If the temperature is lower than 0 ° C, the dehydration reaction is difficult to proceed,
If the temperature exceeds ℃, the amount of polymer produced increases. The organic solvent azeotroped with the produced water is immediately cooled and phase-separated, and then returned to the reaction system again to carry out the reaction.

【0014】(後処理法)反応終了後、有機溶媒反応液
中に含まれる、生成したマレイミド1重量部に対し、
0.1〜20重量部、好ましくは0.3〜10重量部の
水を加えて、攪拌後、静置し、油水分離して洗浄する。
攪拌は、一般に、回転数30〜300rpmで、3〜3
0分間攪拌することにより行われる。洗浄は、20〜9
5℃の温度範囲で、1〜5回、好ましくは2回以上行
う。水洗後、溶媒を留去し、実質的に溶媒が無くなるま
で留去して、マレイミドを溶融状態で抜き出すか、また
は、水、メタノール、エタノール等のマレイミドに対し
て、貧溶媒を添加して、結晶状態で取り出すことによ
り、高純度マレイミドを得る。
(Post-treatment method) After the reaction, with respect to 1 part by weight of the produced maleimide contained in the organic solvent reaction solution,
0.1 to 20 parts by weight, preferably 0.3 to 10 parts by weight of water is added, and after stirring, the mixture is allowed to stand, separated from oily water, and washed.
Stirring is generally 3 to 3 at a rotation speed of 30 to 300 rpm.
It is performed by stirring for 0 minutes. Washing is 20-9
It is performed 1 to 5 times, preferably 2 or more times, in a temperature range of 5 ° C. After washing with water, the solvent is distilled off, until substantially no solvent is removed, or maleimide is extracted in a molten state, or water, methanol, with respect to maleimide such as ethanol, by adding a poor solvent, High-purity maleimide is obtained by taking out in a crystalline state.

【0015】[0015]

【実施例】以下、実施例により本発明を詳細に説明す
る。 実施例1 冷却器、温度計、攪拌機および水分離器を備えた500
mlの四口フラスコ内に、4,4′−メチレンジアニリ
ン40g、酢酸n−ブチル280gおよび、N−メチル
−2−ピロリドン10gを仕込み内温を20℃に調整し
ながら溶解させた。次に無水マレイン酸43.6gを少
量ずつ30分かけて添加し、終了後、更に30分間攪拌
した。続いて、パラトルエンスルホン酸3.8gを添加
後昇温し、温度128℃に4時間保ち反応を遂行した。
この間に生成した水は酢酸n−ブチルとともに系外へ留
去せしめた。
The present invention will be described in detail below with reference to examples. Example 1 500 with cooler, thermometer, stirrer and water separator
In a ml four-necked flask, 40 g of 4,4'-methylenedianiline, 280 g of n-butyl acetate and 10 g of N-methyl-2-pyrrolidone were charged and dissolved while adjusting the internal temperature to 20 ° C. Next, 43.6 g of maleic anhydride was added little by little over 30 minutes, and after the completion, stirring was continued for 30 minutes. Subsequently, 3.8 g of para-toluenesulfonic acid was added and the temperature was raised, and the temperature was kept at 128 ° C. for 4 hours to carry out the reaction.
The water generated during this time was distilled out of the system together with n-butyl acetate.

【0016】反応終了後、純水200gで3回洗浄し、
次いで、温度80℃に保持した油浴中、減圧下(100
〜20mmHg)で酢酸n−ブチルを210g留去し
た。反応液を50℃まで冷却後、メタノール250gを
反応液中に添加しスラリー液を得た。これを濾別し、乾
燥して、淡黄色のビスマレイミド粉末67.2gを得
た。(収率92.9%)このビスマレイミドのキャピラ
リー法による融点は156〜159℃、液体クロマトグ
ラフ(示差屈折率検出器)の面積百分率で測定した純度
は94.8%、N/10KOHエタノール溶液で滴定し
た酸価3.0(mg・KOH/g)であった。
After the reaction was completed, the product was washed with 200 g of pure water three times,
Then, in an oil bath maintained at a temperature of 80 ° C, under reduced pressure (100
210 g of n-butyl acetate was distilled off at ˜20 mmHg). After cooling the reaction solution to 50 ° C., 250 g of methanol was added to the reaction solution to obtain a slurry solution. This was separated by filtration and dried to obtain 67.2 g of pale yellow bismaleimide powder. (Yield 92.9%) The melting point of this bismaleimide by the capillary method is 156 to 159 ° C., the purity measured by the area percentage of the liquid chromatograph (differential refractive index detector) is 94.8%, and the N / 10KOH ethanol solution is used. The acid value was 3.0 (mgKOH / g).

【0017】比較例1 実施例1と同様の装置を具備したフラスコ内に4,4′
−メチレンジアニリン40g及びアセトン230gを入
れ内温を20℃に調整した。次に無水マレイン酸43.
6gを少量ずつ30分間かけて添加し、終了後、更に3
0分間攪拌した。続いて、無水酢酸54g、トリエチル
アミン10ml、酢酸ニッケル0.4gを添加後昇温し
65℃で2時間反応を遂行した。
Comparative Example 1 4,4 'was placed in a flask equipped with the same apparatus as in Example 1.
-Methylenedianiline (40 g) and acetone (230 g) were added to adjust the internal temperature to 20 ° C. Then maleic anhydride 43.
Add 6g little by little over 30 minutes, then add 3 more
Stir for 0 minutes. Subsequently, 54 g of acetic anhydride, 10 ml of triethylamine and 0.4 g of nickel acetate were added and the temperature was raised to carry out a reaction at 65 ° C. for 2 hours.

【0018】反応終了後、室温まで冷却し、反応溶液を
1000mlの純水中に滴下し、結晶を析出させた。結
晶を濾別後、純水1000mlで2回洗浄を行い乾燥
し、黄色のビスマレイミド67.5gを得た。(収率9
3.3%)このビスマレイミドの融点は143〜148
℃、純度88.0%、酸価11.5(mg・KOH/
g)であった。
After completion of the reaction, the reaction solution was cooled to room temperature, and the reaction solution was dropped into 1000 ml of pure water to precipitate crystals. The crystals were separated by filtration, washed twice with 1000 ml of pure water and dried to obtain 67.5 g of yellow bismaleimide. (Yield 9
3.3%) The melting point of this bismaleimide is 143-148.
℃, purity 88.0%, acid value 11.5 (mg · KOH /
g).

【0019】比較例2 冷却器、温度計、攪拌機および水分離器を備えた500
mlの四口フラスコ内に4,4′−ジアミノジフェニル
メタン40g、トルエン250gおよびN−メチル−2
−ピロリドン10g仕込み内温を20℃に調整しながら
溶解させた。次にマレイン酸43.6gを少量ずつ30
分かけて添加し、終了後、更に30分間攪拌した。続い
て、パラトルエンスルホン酸3.8gを添加後昇温し、
温度112℃に5時間保ち反応を遂行した。この間に生
成した水はトルエンとともに系外へ留去せしめた。反応
終了後、純水200gで1回洗浄したところ、ビスマレ
イミドの粘稠物が析出してしまい、油水分離不能となっ
たため、以降の操作を行わなかった。
Comparative Example 2 500 equipped with a cooler, thermometer, stirrer and water separator
In a ml four-necked flask, 40 g of 4,4'-diaminodiphenylmethane, 250 g of toluene and N-methyl-2.
-Pyrrolidone 10 g was dissolved while adjusting the internal temperature to 20 ° C. Next, maleic acid (43.6 g) is added in small amounts to 30
The mixture was added over a period of minutes, and after completion, the mixture was stirred for another 30 minutes. Subsequently, 3.8 g of paratoluenesulfonic acid was added and the temperature was raised,
The reaction was carried out by keeping the temperature at 112 ° C. for 5 hours. Water generated during this time was distilled out of the system together with toluene. After completion of the reaction, the product was washed once with 200 g of pure water, and a viscous bismaleimide was deposited, which made it impossible to separate oil and water. Therefore, the subsequent operations were not performed.

【0020】実施例2〜6 アミンの種類、溶媒、酸触媒および反応温度を表1のよ
うに変えた他は実施例1と同様にしてマレイミドを得
た。結果を表1にまとめて示す。
Examples 2 to 6 Maleimides were obtained in the same manner as in Example 1 except that the kind of amine, solvent, acid catalyst and reaction temperature were changed as shown in Table 1. The results are summarized in Table 1.

【0021】[0021]

【表1】 [Table 1]

【0022】*1:4,4’−メチレンジアニリン *2:2,2’−ビス〔4−(4−アミノフェノキシ)
フェニル〕プロパン *3:3,3′−ジエチル−5,5′ジメチル−4,
4′−ジアミノジフェニルメタン *4:メタフェニレンジアミン *5:アニリンとホルムアルデヒドから得られるポリア
ミン、三井東圧(株)製品名 *6:アニリン4モル、O−トルイジン4モル、テレフ
タルアルデヒド1モルから得れるポリアミン *7:酢酸ブチル *8:N−メチル−2−ピロリドン *9:酢酸エチル *10:ジメチルホルムアミド *11:プロピオン酸ブチル *12:ジメチルアセトアミド *13:パラトルエンスルホン酸
* 1: 4,4'-methylenedianiline * 2: 2,2'-bis [4- (4-aminophenoxy)
Phenyl] propane * 3: 3,3'-diethyl-5,5'dimethyl-4,
4'-Diaminodiphenylmethane * 4: Metaphenylenediamine * 5: Polyamine obtained from aniline and formaldehyde, Mitsui Toatsu Co., Ltd. product name * 6: Obtained from aniline 4 mol, O-toluidine 4 mol, terephthalaldehyde 1 mol Polyamine * 7: Butyl acetate * 8: N-methyl-2-pyrrolidone * 9: Ethyl acetate * 10: Dimethylformamide * 11: Butyl propionate * 12: Dimethylacetamide * 13: Paratoluenesulfonic acid

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 アミン類と無水マレイン酸とを、エステ
ル溶媒と非プロトン性極性溶媒の混合溶媒中で反応させ
てマレアミド酸を得、該マレアミド酸を、酸触媒の存在
下、脱水閉環反応させることを特徴とするマレイミドの
製造方法。
1. A maleic acid is obtained by reacting an amine with maleic anhydride in a mixed solvent of an ester solvent and an aprotic polar solvent, and the maleamic acid is subjected to a dehydration ring-closing reaction in the presence of an acid catalyst. A method for producing a maleimide, comprising:
【請求項2】 エステル溶媒が、一般式R1 COOR2
〔式中、R1 は水素原子または炭素数1〜8のアルキル
基を示し、R2 は炭素数1〜10のアルキル基を示
す。〕で表されるものである請求項1に記載の方法。
2. The ester solvent is of the general formula R 1 COOR 2
[In the formula, R 1 represents a hydrogen atom or an alkyl group having 1 to 8 carbon atoms, and R 2 represents an alkyl group having 1 to 10 carbon atoms. ] The method of Claim 1 represented by these.
【請求項3】 非プロトン性極性溶媒が、アミド系溶媒
である請求項1に記載の方法。
3. The method according to claim 1, wherein the aprotic polar solvent is an amide solvent.
【請求項4】 酸触媒が、有機酸触媒である請求項1記
載の方法。
4. The method according to claim 1, wherein the acid catalyst is an organic acid catalyst.
JP4167645A 1992-06-25 1992-06-25 Production of maleimide Pending JPH069556A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4167645A JPH069556A (en) 1992-06-25 1992-06-25 Production of maleimide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4167645A JPH069556A (en) 1992-06-25 1992-06-25 Production of maleimide

Publications (1)

Publication Number Publication Date
JPH069556A true JPH069556A (en) 1994-01-18

Family

ID=15853610

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4167645A Pending JPH069556A (en) 1992-06-25 1992-06-25 Production of maleimide

Country Status (1)

Country Link
JP (1) JPH069556A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997047597A1 (en) * 1996-06-14 1997-12-18 Hos-Technik Process for preparation of twice-unsaturated bis-imides with a high level of colour stability and a low level of polymers
JP2003055342A (en) * 2001-08-21 2003-02-26 Mitsui Chemicals Inc Method for producing maleimide compound
WO2007034590A1 (en) 2005-09-26 2007-03-29 Olympus Medical Systems Corp. Ultrasonograph

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997047597A1 (en) * 1996-06-14 1997-12-18 Hos-Technik Process for preparation of twice-unsaturated bis-imides with a high level of colour stability and a low level of polymers
JP2003055342A (en) * 2001-08-21 2003-02-26 Mitsui Chemicals Inc Method for producing maleimide compound
WO2007034590A1 (en) 2005-09-26 2007-03-29 Olympus Medical Systems Corp. Ultrasonograph

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