JPS5952660B2 - Polymaleimide manufacturing method - Google Patents

Polymaleimide manufacturing method

Info

Publication number
JPS5952660B2
JPS5952660B2 JP51096948A JP9694876A JPS5952660B2 JP S5952660 B2 JPS5952660 B2 JP S5952660B2 JP 51096948 A JP51096948 A JP 51096948A JP 9694876 A JP9694876 A JP 9694876A JP S5952660 B2 JPS5952660 B2 JP S5952660B2
Authority
JP
Japan
Prior art keywords
cobalt
acid
bismaleimide
phenylene
polymaleimide
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
Application number
JP51096948A
Other languages
Japanese (ja)
Other versions
JPS5323396A (en
Inventor
貴達 下川
宗弘 河内
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP51096948A priority Critical patent/JPS5952660B2/en
Publication of JPS5323396A publication Critical patent/JPS5323396A/en
Publication of JPS5952660B2 publication Critical patent/JPS5952660B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Electric Clocks (AREA)
  • Pyrrole Compounds (AREA)

Description

【発明の詳細な説明】 本発明の目的は重合活性の優れたポリマレイミドを高収
率で得る製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION An object of the present invention is to relate to a method for producing a polymaleimide having excellent polymerization activity in high yield.

ポリマレイミドとは分子内にマレイミド基を2ケ以上含
む比較的低分子の化合物、いわゆるオリゴマ−であり、
単独又は他の適当なモノマーと組合せて、熱又は触媒に
より重合反応を起し、いわゆる三次元構造を主体とする
熱硬化性樹脂の硬化物を形成する。
Polymaleimide is a relatively low-molecular compound containing two or more maleimide groups in the molecule, a so-called oligomer.
Either alone or in combination with other suitable monomers, a polymerization reaction is caused by heat or a catalyst to form a cured thermosetting resin mainly having a so-called three-dimensional structure.

このポリマレイミドを含む熱硬化性樹脂の硬化物は耐熱
性が優れており、耐熱性の要求される電気、機械分野に
おいてワニス、粉体塗料、積層板、成型物等として利用
されている。このような用途にポリマレイミドを含む熱
硬化性樹脂を使用する場合、その重合硬化反応が迅速且
つ充分に進行する事が硬化物製造の生産性を高める上で
も又、硬化物に良好な耐熱性を附与する上でも必要とさ
れるが、この条件を満たす為には、原料として用いるポ
リマレイミドの重合活性が高い事が必要とされる。ポリ
マレイミドはこのように有用であるので、従来より重合
活性の高いポリマレイミドを高収率で安価に製造する方
法の開発が望まれている。従来ポリマレイミドの一種で
あるビスマレイミドの製造法については、例えばNat
i0na15AMPE5ymp0siumExhib1
8284〜291(1973)に記載されているように
一例として4、4’−ジアミノジフェニルメタンの如き
第一級ジアミン1モルと無水マレイン酸2モルとをジメ
チルホルムアミドの如き有機溶媒中、1.1モルの酢酸
ナトリウム存在下に1式の如く開環附加させて、N、N
’一(メチレンジーP−フェニレン)ビスマレアミド酸
とし、次にこれに脱水剤として、2モルの無水酢酸を添
加して2式の如く脱水環化させてN、N’一(メチレン
ジーP−フェニレン)ビスマレイミドの如きビスマレイ
ミドが得られるフことは公知となつている。
Cured products of thermosetting resins containing this polymaleimide have excellent heat resistance and are used as varnishes, powder coatings, laminates, molded products, etc. in electrical and mechanical fields where heat resistance is required. When using a thermosetting resin containing polymaleimide for such applications, it is important that the polymerization and curing reaction proceed quickly and sufficiently to increase the productivity of manufacturing the cured product, and also to ensure that the cured product has good heat resistance. In order to satisfy this condition, the polymerization activity of the polymaleimide used as a raw material is required to be high. Since polymaleimide is useful in this way, there is a desire to develop a method for producing polymaleimide with higher polymerization activity at a higher yield and at a lower cost than ever before. Regarding the production method of bismaleimide, which is a type of polymaleimide, for example, Nat
i0na15AMPE5ymp0siumExhib1
8284-291 (1973), for example, 1 mol of a primary diamine such as 4,4'-diaminodiphenylmethane and 2 mol of maleic anhydride are mixed in 1.1 mol in an organic solvent such as dimethylformamide. In the presence of sodium acetate, N,N
'-(methylene di-P-phenylene) bismaleamic acid was prepared, and then 2 moles of acetic anhydride was added as a dehydrating agent to dehydrate and cyclize it as shown in formula 2 to form N,N'-(methylene di-P-phenylene) bis. It is known that bismaleimides such as maleimide can be obtained.

この公知の方法により、例えば4,4″−ジアミノジフ
エニルメタンと無水マレイン酸とを反応させて得られる
N,N″一(メチレンジ一P−フエニレン)ビスマレア
ミド酸からN,N″−(メチレンジ一P−フエニレン)
ビスマレイミドを製造すると、淡黄色粉末で、重合活性
の高い前記ビスマレイミドが得られる。
By this known method, for example, N,N''-(methylenedi-1P-phenylene)bismaleamic acid obtained by reacting 4,4''-diaminodiphenylmethane with maleic anhydride is converted into N,N''-(methylenedi-1P-phenylene)bismaleamic acid. P-phenylene)
When bismaleimide is produced, the bismaleimide is obtained as a pale yellow powder with high polymerization activity.

しかしながら、この公知の方法によれば得られる前記ビ
スマレイミドの原料ビスマレアミド酸に対する収率(以
下、単に収率と称す)75〜80%と低く、工業的な実
用性に乏しかつた。この為ビスマレイミドの製造法に関
して種々の研究が行われ、その後触媒として可溶性ニツ
ケル化合物の存在下、ビスマレアミド酸と力ルボン酸無
水物を反応させる事により対応するビスマレイミドを製
造する方法が公知となつている。この公知の方法により
例えば4,4″−ジアミノジフエニルメタンに無水マレ
イン酸を附加して得られるN,N″−(メチレンジ一P
−フエニレ.ン)ビスマレインアミド酸からN,N″−
(メチレンジ一P−フエニレン)ビスマレイミドを製造
した場合、収率は約85%と比較的高いが得られた上記
ビスマレイミドは着色が著しく茶褐色を呈しており、酢
酸ナトリウム触媒による前記ビスマレ3イミドに較べて
重合活性が低い。又、触媒としてアルカリ土類金属化合
物を使用することを特徴とするビスマレイミドの製造法
が特開昭50−83368に開示されている。
However, according to this known method, the yield of the bismaleimide obtained with respect to the raw material bismaleamic acid (hereinafter simply referred to as yield) is as low as 75 to 80%, and it lacks industrial practicality. For this reason, various studies were conducted on methods for producing bismaleimide, and subsequently, a method for producing the corresponding bismaleimide by reacting bismaleamic acid and carboxylic acid anhydride in the presence of a soluble nickel compound as a catalyst became known. ing. By this known method, for example, N,N''-(methylenedi-P) is obtained by adding maleic anhydride to 4,4''-diaminodiphenylmethane.
- Phoenix. ) from bismaleamic acid to N,N''-
When (methylenedi-P-phenylene) bismaleimide is produced, the yield is relatively high at about 85%, but the obtained bismaleimide has a marked brownish color, and the bismaleimide produced by the sodium acetate catalyst has a relatively high yield of about 85%. Polymerization activity is low compared to that of Further, a method for producing bismaleimide characterized by using an alkaline earth metal compound as a catalyst is disclosed in JP-A-50-83368.

本発明者らは上記製造法により4,4″−ジアミノジフ
エニル・メタンと無水マレイン酸を付加させて得たN,
N′一(メチレンジ一P−フエニレン)ビスマレアミド
酸に無水酢酸を脱水剤とし、触媒として酢酸カルシウム
を用いて反応を行なつたところ、91%の高収率でN,
N″−(メチレンジ一P−フエニレン)ビスマレイミド
が得られた。しかしながら、得られた上記ビスマレイミ
ドは黒褐色を呈しており、重合活性は非常に低かつた。
一般に熱硬化性樹脂の硬化物は、ビスマレイミドから得
られる硬化性樹脂の硬化物も含めて、架橋硬化反応を充
分に行わせた、いわゆる架橋密度の高い硬化物は硬化不
充分の硬化物に較べて機械的強度、耐薬品性、耐熱性が
優れていることは公知の事実であるが、本発明者らの研
究によれば重合活性の低いビスマレイミドから得られる
硬化性樹脂は、これを加熱硬化させても、硬化反応が充
分に進行しない為であろうか、得られる硬化物は、重合
活性の高いビスマレイミドを用いた場合に較べて、機械
的強度、耐薬品性、耐熱性が劣ることがわかつた。
The present inventors obtained N,
When N'-(methylenedi-1P-phenylene)bismaleamic acid was reacted with acetic anhydride as a dehydrating agent and calcium acetate as a catalyst, N,
N''-(methylenedi-P-phenylene) bismaleimide was obtained. However, the obtained bismaleimide had a blackish brown color and had very low polymerization activity.
In general, cured products of thermosetting resins, including cured products of curable resins obtained from bismaleimide, are cured products that have sufficiently undergone crosslinking and curing reactions, so-called cured products with a high crosslinking density, and cured products that are insufficiently cured. It is a well-known fact that the curable resin obtained from bismaleimide, which has low polymerization activity, has superior mechanical strength, chemical resistance, and heat resistance. Perhaps this is because the curing reaction does not proceed sufficiently even after heat curing, but the resulting cured product has poorer mechanical strength, chemical resistance, and heat resistance than when bismaleimide, which has high polymerization activity, is used. I found out.

又重合活性の低いビスマレイミドから得られる硬化性樹
脂の硬化を充分に進めるべく、より高温度で長時間の熱
処理を行つてみたが、熱劣化が起る為か、得られる硬化
物はやはり重合活性の高いビスマレイミドを用いた場合
に較べて、機械的強度、耐薬品性、耐熱性が劣ることが
わかつた。即ち、以上に述べた如く重合活性の優れたビ
スマレイミドを少なくとも85%、望ましくは90%以
上の収率で得られる製造法が見出され・ば、工業的価値
は非常に高いものである。
In addition, in order to sufficiently cure the curable resin obtained from bismaleimide, which has low polymerization activity, we performed heat treatment at a higher temperature for a longer time, but the resulting cured product still did not polymerize, perhaps due to thermal deterioration. It was found that mechanical strength, chemical resistance, and heat resistance were inferior to those using highly active bismaleimide. That is, if a production method capable of producing bismaleimide with excellent polymerization activity at a yield of at least 85%, preferably 90% or more, as described above, could be found, it would be of great industrial value.

本発明者らは重合活性が優れ、かつ高収率でポリマレイ
ミドを製造する方法について鋭意研究した結果、触媒と
してコバルト化合物を使用することにより重合活性の優
れたポリマレイミドを高収率で得られる事を見出し、本
発明を達成した。
The present inventors have conducted intensive research on a method for producing polymaleimide with excellent polymerization activity and high yield, and have found that by using a cobalt compound as a catalyst, polymaleimide with excellent polymerization activity can be obtained in high yield. They discovered this and achieved the present invention.

本発明はポリマレインアミド酸を脱水剤、コバルト化合
物、第三級アミンの存在下で反応させることを特徴とす
るポリマレイミドの製造方法である。本発明において脱
水環化反応の触媒として用いられるコバルト化合物とは
、反応媒体に可溶な2価又は3価のコバルト化合物を意
味し、その例としては、場合により水和した形の2価の
コバルト塩、例えば塩化物、臭化物、沃化物、フツ化物
、ギ酸塩、酢酸塩、プロピオン酸塩、酪酸塩、ステアリ
ン酸塩、リノール酸塩、ナフテン酸塩、安息,香酸塩、
炭酸塩、硫酸塩、硝酸塩、燐酸塩、水酸化塩、過塩素酸
塩など、又場合により水和した形の3価コバルト塩、例
えば塩化物、臭化物、沃化物、フツ化物、ギ酸塩、酢酸
塩、プロピオン酸塩、硫酸塩など、又2価のコバルト錯
塩、例えばコバルト−ビスアセチルアセトナート、テト
ラキズ(ピリジン)コバルト塩化物など、および3価の
コバルト錯塩、例えばコバルトトリスアセチルアセトナ
ート、トリス(ジピリジル)コバルト塩化物などをあげ
ることができる。
The present invention is a method for producing polymaleimide, which is characterized by reacting polymaleamide acid in the presence of a dehydrating agent, a cobalt compound, and a tertiary amine. The cobalt compound used as a catalyst for the cyclodehydration reaction in the present invention means a divalent or trivalent cobalt compound soluble in the reaction medium, such as a divalent cobalt compound optionally in hydrated form. Cobalt salts such as chloride, bromide, iodide, fluoride, formate, acetate, propionate, butyrate, stearate, linoleate, naphthenate, benzoate, framate,
trivalent cobalt salts such as carbonates, sulphates, nitrates, phosphates, hydroxides, perchlorates, and optionally in hydrated form, such as chlorides, bromides, iodides, fluorides, formates, acetic acid salts, propionates, sulfates, etc., as well as divalent cobalt complex salts, such as cobalt-bisacetylacetonate, tetrakiz(pyridine)cobalt chloride, etc., and trivalent cobalt complex salts, such as cobalt trisacetylacetonate, tris( Dipyridyl) cobalt chloride, etc.

反応後の精製の容易さの点で2価の酢酸コバルト、ナフ
テン酸コバルトまたは安息香酸コバルトを使用すること
が好ましい。触媒の使用量はマレアミド酸基1当量当り
2×10−5〜0.2当量の範囲、好ましくは2X10
−4〜2×10−2当量の範囲の極少量でよい。本発明
における脱水剤とはマレアミド酸基に作用してこれを脱
水環化させてマレイミド基に変え、自身は水和物となる
もので、例えば無水酢酸、無水プロピオン酸、無水酪酸
、無水吉草酸、等の低級モノカルボン酸無水物。又無水
コハク酸、無水グルタル酸、無水フタル酸等のジカルボ
ン酸無水物。又酸化カルシウム、酸化バリウム等の酸化
物をあげることができる。通常脱水剤としては無水酢酸
が経済性及び反応後ポリマレイミドの精製が容易な点で
好ましい。この脱水剤の使用量はマレアミド酸基1当量
当り脱水剤1〜5モル、好ましくは1.1〜2.2モル
の範囲である。本発明において使用される第三級アミン
としては、例えば、トリメチルアミン、トリエチルアミ
ン、トリ−n−ブチルアミン等の炭素数1〜10のアル
キル基を有するトリアルキルアミン類、又N,N″−ジ
メチルベンジルアミン、N,N−ジエチルベンジルアミ
ン等のN,N−ジアルキルベンジルアミン類、及び1,
8−ジアザビシクロ〔5,4,0〕 7ーウンデセン、
N−メチルモルホリン、N−エチルモルホリン等の環状
アミン類を用いることができる。特に好ましい第三級ア
ミンは、トリエチルアミンである。第三級アミンの使用
量は、マレインアミド酸基1当量当り0.01〜2.0
モルの範囲、好ましくは、0.1〜0.5モルの範囲で
゛ある。本発明における脱水環化反応は、20〜100
℃の範囲の温度で好ましくは40〜60℃の範囲の温度
で、反応系が液相になる圧力の下で行なわれる。
From the viewpoint of ease of purification after the reaction, it is preferable to use divalent cobalt acetate, cobalt naphthenate, or cobalt benzoate. The amount of catalyst used is in the range of 2 x 10-5 to 0.2 equivalents per equivalent of maleamic acid group, preferably 2 x 10
A very small amount in the range of −4 to 2×10 −2 equivalents is sufficient. In the present invention, the dehydrating agent is one that acts on maleamic acid groups to dehydrate and cyclize them to convert them into maleimide groups, and itself becomes a hydrate, such as acetic anhydride, propionic anhydride, butyric anhydride, valeric anhydride. , etc. lower monocarboxylic acid anhydrides. Also, dicarboxylic acid anhydrides such as succinic anhydride, glutaric anhydride, and phthalic anhydride. Further, oxides such as calcium oxide and barium oxide can be mentioned. Generally, acetic anhydride is preferred as the dehydrating agent because of its economical efficiency and ease of purification of the polymaleimide after reaction. The amount of the dehydrating agent used is in the range of 1 to 5 mol, preferably 1.1 to 2.2 mol, of the dehydrating agent per equivalent of maleamic acid group. Examples of the tertiary amine used in the present invention include trialkylamines having an alkyl group having 1 to 10 carbon atoms, such as trimethylamine, triethylamine, and tri-n-butylamine, and N,N''-dimethylbenzylamine. , N,N-dialkylbenzylamines such as N,N-diethylbenzylamine, and 1,
8-diazabicyclo[5,4,0] 7-undecene,
Cyclic amines such as N-methylmorpholine and N-ethylmorpholine can be used. A particularly preferred tertiary amine is triethylamine. The amount of tertiary amine used is 0.01 to 2.0 per equivalent of maleamic acid group.
It is in the molar range, preferably in the range of 0.1 to 0.5 molar. The dehydration cyclization reaction in the present invention is carried out at 20 to 100
The reaction is carried out at a temperature in the range of 0.degree. C., preferably in the range of 40 to 60.degree. C., under a pressure such that the reaction system is in a liquid phase.

本発明において必要に応じて使用される有機溶媒として
は、例えばジメチルホルムアミド、ジメチルアセトアミ
ド、ジメチルスルホキシド、Nメチノレピロリドン、N
−メチノレカプロラクタムのような極性溶媒、又テトラ
ヒドロフラン、ジオキサンのような環状エーテル化合物
、又特に有利な溶媒はアセトン、メチルエチルケトンの
ようなジアルキルケトン類である。有機溶媒の使用量は
、ポリマレアミド酸重量の1.0〜4.0倍重量が好ま
しい。又脱水剤である無水酢酸、無水酪酸等の低級カル
ボン酸は溶媒としての機能を有するので、とくに有機溶
媒を使用せずに反応を進行させることが可能である。本
発明はこのように有機希釈剤を使用しない方法をも包含
するものである。本発明の方法において出発物質として
用いることが出来るポリマレインアミド酸とはマレイン
アミド酸基を分子内に2ケ以上含有する化合物を意味し
、例えば、N−N″−(m−フエニレン)ビスマレアミ
ド酸、N−N″−(メチレンジ一Pフエニレン)ビスマ
レアミド酸、N,N″−(オキシジ一P−フエニレン)
ビスマレアミド酸、N,N′一(スルホニルジ一m−フ
エニレン)ビスマレアミド酸、N,N″−(スルホニル
ジ一Pフエニレン)ビスマレアミド酸、N,N″(イソ
プロピリデンジ一P−フエニレン)ビスマレアミド酸、
N,N″−〔メチレンジ一(3−クロロ1,4−フエニ
レン)〕ビスマレアミド酸、N,N″−(4−メチル1
,3−フエニレンビスノマレアミド酸、N,N″−(2
−メチル−1,3フエニレン)ビスマレアミド酸等のビ
スマレアミド酸、又式(1)で示される2価より大きな
多価マレアミド酸をあげることが出来る。
Examples of organic solvents used as necessary in the present invention include dimethylformamide, dimethylacetamide, dimethyl sulfoxide, N-methylepyrrolidone, N-
- Polar solvents, such as methynolecaprolactam, and also cyclic ether compounds, such as tetrahydrofuran, dioxane, and particularly preferred solvents are dialkyl ketones, such as acetone, methyl ethyl ketone. The amount of organic solvent used is preferably 1.0 to 4.0 times the weight of the polymaleamic acid. Further, lower carboxylic acids such as acetic anhydride and butyric anhydride, which are dehydrating agents, have a function as a solvent, so that it is possible to proceed the reaction without particularly using an organic solvent. The present invention thus also includes methods that do not use organic diluents. The polymaleamic acid that can be used as a starting material in the method of the present invention refers to a compound containing two or more maleamic acid groups in the molecule, such as N-N''-(m-phenylene)bismaleamic acid. , N-N″-(methylenedi-P-phenylene) bismaleamic acid, N,N″-(oxydi-P-phenylene)
Bismaleamic acid, N,N′-(sulfonyldi-1m-phenylene)bismaleamic acid, N,N″-(sulfonyldi-1P-phenylene)bismaleamic acid, N,N″(isopropylidenedi-1P-phenylene)bismaleamic acid,
N,N″-[methylenedi-(3-chloro-1,4-phenylene)]bismaleamic acid, N,N″-(4-methyl-1
,3-phenylenebisnomaleamic acid, N,N''-(2
-Methyl-1,3phenylene) bismaleamic acid, and polyvalent maleamic acids with a higher valence than the divalent one represented by the formula (1) can be mentioned.

本発明の出発原料であるポリマレアミド酸は公知の方法
に準じて無水マレイン酸に対応するポリアミンを適当な
有機溶剤の存在下に作用させることによつてほぼ理論量
の収量で製造することができる。
Polymaleamic acid, which is the starting material of the present invention, can be produced in approximately the theoretical yield by reacting a polyamine corresponding to maleic anhydride in the presence of a suitable organic solvent according to a known method.

本発明の製造法を有利に実施するにはこのように有機溶
剤中で無水マレイン酸とポリアミンと付加反応させて得
られるポリマレアミド酸を分離することなく本発明の製
造法である脱水環化反応に直接用いることである。本発
明の製造方法によればポリマレイミドが収率90%以上
の高収率で製造する事が出来、しかも得られたポリマレ
イミドは淡黄色で重合活性が高く、特にビスマレイミド
を配合した硬化性樹脂は短時間で硬化でき、得られた硬
化物は機械的性質、電気的特性及び耐熱性の優れたもの
であつた。
In order to advantageously carry out the production method of the present invention, the polymaleamic acid obtained by the addition reaction of maleic anhydride and a polyamine in an organic solvent can be subjected to the dehydration cyclization reaction, which is the production method of the present invention, without separating it. It is to be used directly. According to the production method of the present invention, polymaleimide can be produced at a high yield of 90% or more, and the obtained polymaleimide is pale yellow in color and has high polymerization activity, and is especially curable when bismaleimide is blended. The resin could be cured in a short time, and the cured product obtained had excellent mechanical properties, electrical properties, and heat resistance.

以下本発明の態様を実施例により具体的に説明する。し
かし、本発明はこれに限定されるものではない。なお実
施例においてポリマレイミドのゲル化時間は次のように
して測定し、これを重合活性の指標とした。
Hereinafter, aspects of the present invention will be specifically explained with reference to Examples. However, the present invention is not limited thereto. In the examples, the gelation time of polymaleimide was measured as follows, and this was used as an index of polymerization activity.

ゲル化時間が短かい程重合活性が高いと云える。即ちポ
リマレイミド、サンプル1gを200℃±1℃に調節し
たステンレス盤上に載せ、ステンレス製ヘラで1秒間に
1回づつ練り、サンプルがゲル状になる迄の時間をゲル
化時間とした。ゲル化時間は3分以下であることが実用
上望.ましく更に望ましくは1分以下である。実施例
1 N,N″−(メチレンジ一P−フエニレン)ビスマレア
ミド酸98.5g(4).25モル)をアセトン250
gに溶解させた。
It can be said that the shorter the gelation time, the higher the polymerization activity. That is, 1 g of a sample of polymaleimide was placed on a stainless steel plate adjusted to 200° C.±1° C., and kneaded once per second with a stainless steel spatula, and the time until the sample became gel-like was defined as the gelation time. Practically speaking, it is desirable that the gelation time be 3 minutes or less. More preferably, it is 1 minute or less. Example
1 N,N″-(methylenedi-P-phenylene) bismaleamic acid (98.5 g (4).25 mol) was dissolved in acetone 250 g.
It was dissolved in g.

これにナフテン酸コバルト0.63g(2.0ミリモル
)、トリエチルアミン10g(4).1モル)、無水酢
酸71.4g(イ).7モル)を添加した後反応温度を
55℃に上げ60℃以下に保ちながら2時間反応させた
To this was added 0.63 g (2.0 mmol) of cobalt naphthenate and 10 g (4) of triethylamine. 1 mol), acetic anhydride 71.4 g (a). After adding 7 mol), the reaction temperature was raised to 55°C, and the reaction was continued for 2 hours while maintaining the temperature below 60°C.

次に20℃に冷却し、この溶液に水250gを滴下し沈
澱する固体を濾別した。この沈澱を水洗し次に炭酸ソー
ダ水溶液で洗浄し、更に水洗し、最後にメタノールで洗
浄後乾燥し、N,N″−(メチレンジ一P−フエニレン
)ビスマレイミド81.5g(収率91%)の淡黄色粉
末を得た。この淡黄色粉末のゲル化時間を測定した所4
0秒でゲル化した。実施例 2 触媒として安息香酸コバルト0.6g(2.0ミリモル
)使用する以外実施例1と全く同じ方法及びスケールで
行つた。
Next, the solution was cooled to 20° C., and 250 g of water was added dropwise to this solution, and the precipitated solid was filtered off. This precipitate was washed with water, then with an aqueous sodium carbonate solution, further washed with water, and finally washed with methanol and dried to obtain 81.5 g of N,N''-(methylenedi-P-phenylene)bismaleimide (yield 91%). A pale yellow powder was obtained.The gelation time of this pale yellow powder was measured.
It gelated in 0 seconds. Example 2 The same method and scale as in Example 1 were used except that 0.6 g (2.0 mmol) of cobalt benzoate was used as a catalyst.

N,N″−(メチレンジ一P−フエニレン)ビスマレイ
ミド80.6g(収率90%)の淡黄色粉末が得られ、
ゲル化時間を測定した所45秒でゲル化した。実施例
3 触媒としてコバルト(自)トリスアセチルアセトネート
0.72g(2.0ミリモル)使用する以外、実施例1
と全く同じ方法及びスケールで行つた。
80.6 g (yield 90%) of pale yellow powder of N,N''-(methylenedi-P-phenylene) bismaleimide was obtained,
The gelation time was measured and gelation occurred in 45 seconds. Example
3 Example 1 except that 0.72 g (2.0 mmol) of cobalt (auto)tris acetylacetonate was used as a catalyst.
It was carried out using exactly the same method and scale.

N,N″−4,4″−ジフエニルメタンビスマレイミド
81.0g(収率90.5%)の淡黄色粉末が得られ、
ゲル化時間を測定した所35秒でゲル化した。実施例
4構造を有するポリマレアミド酸97g(4).1モル
)をアセトン350gに溶解させ、これにナフテン酸コ
バルト0.63g(2.0ミリモル)、トリエチルアミ
1ン10g(0.1モル)無水酢酸71.4g(0.7
モル)を添加した後、反応温度を55℃に上げ60℃以
下を保ちながら2.5時間反応させた。
81.0 g (yield 90.5%) of pale yellow powder of N,N''-4,4''-diphenylmethane bismaleimide was obtained,
The gelation time was measured and gelation occurred in 35 seconds. Example
97g (4) of polymaleamic acid having 4 structures. 1 mol) was dissolved in 350 g of acetone, and in this was dissolved 0.63 g (2.0 mmol) of cobalt naphthenate, 10 g (0.1 mol) of triethylamine, and 71.4 g (0.7 mol) of acetic anhydride.
After adding mol), the reaction temperature was raised to 55°C, and the reaction was continued for 2.5 hours while maintaining the temperature below 60°C.

次に20℃に冷却しこの溶液に水300gを滴下し、沈
澱する固体を炉別した。この沈澱を水洗し次に炭酸ソー
ダ水溶液,で洗浄し、更に水洗して、最後にメタノール
で洗浄後、乾燥し黄褐色の固体77.8g(収率88%
)を得た。赤外吸収スペクトルの測定によりマレイミド
環の存在が確認された。この生成物のゲル化時間を測定
した所32秒でゲル化した。実施例 5 N,N″−(オキシジ一P−フエニレン)ビスマレアミ
ド酸98.9g(イ).25モル)をアセトン300g
に溶解させ、これに酢酸コバルト四水和物0.5g(2
.0ミリモル)、トリエチルアミン10g(4).1、
モル)、無水酢酸71.4g(0.7モル)を添加した
後反応温度を55℃に上げ60℃以下を保ちながら2時
間反応させた。
Next, the solution was cooled to 20° C., 300 g of water was added dropwise to this solution, and the precipitated solid was separated by furnace. This precipitate was washed with water, then with an aqueous sodium carbonate solution, then with water, and finally with methanol, and dried to give 77.8 g of a yellowish brown solid (yield: 88%).
) was obtained. The presence of a maleimide ring was confirmed by infrared absorption spectrum measurement. The gelation time of this product was measured and it gelled in 32 seconds. Example 5 98.9 g (a).25 moles of N,N''-(oxydi-P-phenylene) bismaleamic acid was added to 300 g of acetone.
0.5 g of cobalt acetate tetrahydrate (2
.. 0 mmol), triethylamine 10 g (4). 1,
After adding 71.4 g (0.7 mol) of acetic anhydride, the reaction temperature was raised to 55°C and the reaction was continued for 2 hours while maintaining the temperature at 60°C or lower.

次に20℃に冷却しこの溶液に水250gを滴下し、沈
澱する固体を濾別した。この沈澱を水洗し、次に炭酸ソ
ーダ水溶液で洗浄し、更に水洗して最後にメタノールで
洗浄後乾燥し、N,N″−(オキシジ一P−フエニレン
)ビスマレイミド82.0g(収率91%)の淡黄色粉
末が得られ、ゲル化時間を測定した所43秒でゲル化し
た。実施例 6N,N″−(メチレンジ一P−フエニレ
ン)ビスマレアミド酸98.5g(0.25モル)、ア
セトン250g、酢酸コバルト四水和物0.5g(2.
0ミリモル)、トリエチルアミン10g(0.1モル)
および無水酢酸71.4g(4).7モル)を混合した
後、反応温度を62℃に保持しつつ攪拌を2.5時間続
けた。
Next, the solution was cooled to 20° C., 250 g of water was added dropwise to this solution, and the precipitated solid was filtered off. This precipitate was washed with water, then with an aqueous sodium carbonate solution, further washed with water, finally washed with methanol, and dried to obtain 82.0 g of N,N''-(oxydi-1P-phenylene)bismaleimide (yield 91%). ) was obtained, and gelation occurred in 43 seconds when gelation time was measured. Example 6 98.5 g (0.25 mol) of N,N''-(methylene di-1P-phenylene) bismaleamic acid, acetone 250 g, cobalt acetate tetrahydrate 0.5 g (2.
0 mmol), triethylamine 10g (0.1 mol)
and acetic anhydride 71.4 g (4). After mixing 7 mol), stirring was continued for 2.5 hours while maintaining the reaction temperature at 62°C.

次に25℃に冷却した反応液に水250gを滴下し、沈
澱してきた固体を淵別した。この沈澱を水洗し、炭酸ナ
トリウムで中和し、更に水、およびメタノールで洗浄し
た後乾燥した。N,N″一(メチレンジ一P−フエニレ
ン)ビスマレイミドの淡黄色粉末80.3g(収率89
.6%)が得られ、このもののゲル化時間は42秒であ
つた。実施例 7 N,N′−(メチレンジ一P−フエニレン)ビスマレア
ミド酸98.5g(イ).25モル)、酢酸コバルト四
水和物0.5g(2.0ミリモル)、トリエチルアミン
2g(4).02モル)および無水酢酸21.5g(2
.1モル)を混合攪拌しながら65℃まで加熱し、さら
にトリエチルアミンを8g(イ).08モル)加えて7
2℃まで加熱したところ、暗褐色均一な溶液が得られた
Next, 250 g of water was added dropwise to the reaction solution cooled to 25° C., and the precipitated solid was filtered out. This precipitate was washed with water, neutralized with sodium carbonate, further washed with water and methanol, and then dried. 80.3 g of pale yellow powder of N,N″-(methylenedi-P-phenylene) bismaleimide (yield: 89
.. 6%) was obtained, and the gelation time of this product was 42 seconds. Example 7 98.5 g of N,N'-(methylenedi-P-phenylene)bismaleamic acid (a). 25 mol), cobalt acetate tetrahydrate 0.5 g (2.0 mmol), triethylamine 2 g (4). 02 mol) and acetic anhydride 21.5 g (2
.. 1 mol) was mixed and heated to 65°C with stirring, and further 8 g of triethylamine (a). 08 mol) plus 7
Upon heating to 2°C, a dark brown homogeneous solution was obtained.

72℃で1時間攪拌を続けた後、反応液を室温まで冷却
し、未反応の無水酢酸および生成した酢酸を減圧下に留
去した。
After continuing stirring at 72° C. for 1 hour, the reaction solution was cooled to room temperature, and unreacted acetic anhydride and produced acetic acid were distilled off under reduced pressure.

蒸留残渣に水300gを加え、得られた沈澱を濾別し、
水洗した後、さらに、炭酸ナトリウム溶液で中和し、水
およびメタノールで洗浄後乾燥した。N,N″−(メチ
レンジ一P−フエニレン)ビスマレイミドの淡黄色粉末
64.5g(収率72%)が得られた。ゲル化時間は4
5秒であつた。実施例8〜実施例11 実施例1で使用したN,N″−(メチレンジ一P−フエ
ニレン)ビスマレアミド酸のかわりに、表−1に示した
化合物を使用した他は実施例1と同様に反応を行ない、
表−1に記した結果が得られた。
Add 300 g of water to the distillation residue, filter the resulting precipitate,
After washing with water, it was further neutralized with a sodium carbonate solution, washed with water and methanol, and then dried. 64.5 g (yield 72%) of pale yellow powder of N,N''-(methylenedi-P-phenylene) bismaleimide was obtained.Gelation time was 4.
It was hot in 5 seconds. Examples 8 to 11 The reaction was carried out in the same manner as in Example 1, except that the compounds shown in Table 1 were used instead of N,N''-(methylenedi-P-phenylene) bismaleamic acid used in Example 1. do the
The results shown in Table 1 were obtained.

Claims (1)

【特許請求の範囲】 1 ポリマレアミド酸を脱水剤、コバルト化合物、第三
級アミンの存在下に反応させることを特徴とするポリマ
レイミドの製造方法。 2 コバルト化合物として2価のコバルト塩を使用する
特許請求の範囲第1項記載の方法。 3 コバルト化合物として酢酸コバルト、ナフテン酸コ
バルト、または安息香酸コバルトより選ばれる1種また
は2種以上を使用する特許請求の範囲第1項記載の方法
[Scope of Claims] 1. A method for producing polymaleimide, which comprises reacting polymaleamic acid in the presence of a dehydrating agent, a cobalt compound, and a tertiary amine. 2. The method according to claim 1, wherein a divalent cobalt salt is used as the cobalt compound. 3. The method according to claim 1, wherein the cobalt compound is one or more selected from cobalt acetate, cobalt naphthenate, and cobalt benzoate.
JP51096948A 1976-08-16 1976-08-16 Polymaleimide manufacturing method Expired JPS5952660B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP51096948A JPS5952660B2 (en) 1976-08-16 1976-08-16 Polymaleimide manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP51096948A JPS5952660B2 (en) 1976-08-16 1976-08-16 Polymaleimide manufacturing method

Publications (2)

Publication Number Publication Date
JPS5323396A JPS5323396A (en) 1978-03-03
JPS5952660B2 true JPS5952660B2 (en) 1984-12-20

Family

ID=14178513

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51096948A Expired JPS5952660B2 (en) 1976-08-16 1976-08-16 Polymaleimide manufacturing method

Country Status (1)

Country Link
JP (1) JPS5952660B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0427595U (en) * 1990-06-29 1992-03-04

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH634558A5 (en) * 1978-04-06 1983-02-15 Ciba Geigy Ag METHOD FOR PRODUCING ALIPHATIC N-SUBSTITUTED MALEINIMIDES.
JPS5513234A (en) * 1978-07-17 1980-01-30 Mitsui Toatsu Chem Inc Preparation of polymaleimide
JPS6011900B2 (en) * 1978-07-24 1985-03-28 三井東圧化学株式会社 Polymaleimide manufacturing method
JPS6045642B2 (en) * 1980-09-19 1985-10-11 電気化学工業株式会社 Thermoplastic resin manufacturing method
JPS5896066A (en) * 1981-12-03 1983-06-07 Mitsui Toatsu Chem Inc Preparation of aliphatic maleimide
JPS58217522A (en) * 1982-06-11 1983-12-17 Toray Ind Inc Production of maleimide copolymer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0427595U (en) * 1990-06-29 1992-03-04

Also Published As

Publication number Publication date
JPS5323396A (en) 1978-03-03

Similar Documents

Publication Publication Date Title
DE2657033C2 (en) Crosslinkable mixtures of oligomers or polymers and diamines
JPS5952660B2 (en) Polymaleimide manufacturing method
US4376206A (en) N-Alkenylphenylmaleimides and N,N'-[alkenylene phenylene]bismaleimides for the same
JPH0345617A (en) Straight-chain aromatic poly(amide-imide) having terminal functional group containing latent maleimido functional group, its manufacture, and its use in manufacturing crosslinked polymer
US4500719A (en) Process for the preparation of N-alkenylphenylmaleimides and N,N'-[alkenylenephenylene]bismalemides
US3975401A (en) Process for the dehydration of bis-maleamic acids
EP0051687B1 (en) Maleimides and process for the preparation of same
US4863640A (en) Monomers for high temperature fluorinated polyimides
JPS58109479A (en) Preparation of tetracarboxylic acid anhydride
JPS587620B2 (en) Monomale Imidoid Mataha Polymalein Imidoidino Seizouhouhou
JPH0215084A (en) Fluorine-containing pyromellitic dianhydride and preparation thereof
JPH04214727A (en) Diacetylene based polyamic acid derivative and polyimide
JPH01135765A (en) Novel imide compound and production thereof
US4400521A (en) N-Substituted phenyl maleimides
JPS6135173B2 (en)
JPS6315827A (en) Diacetylene group-containing polyamic acid and polyimide
JP2651219B2 (en) Method for producing curable resin containing imide ring
JPS58174361A (en) Novel aromatic bis-imide and its preparation
JPH0381327A (en) Diacetylenic polyamic acid, derivative thereof, and polyimide
JPS6242908B2 (en)
JPS6366164A (en) Production of bismaleimides
JPS6183158A (en) Preparation of n,n'-m-phenylenebismaleimide
JPS5822113B2 (en) Method for producing bismaleimide
JPS6354438A (en) Molding of diacetylene group-containing polyimide
JPH02172974A (en) Synthesis of bisimide