JP3189520B2 - Method for producing high-purity polymaleimide - Google Patents

Method for producing high-purity polymaleimide

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Publication number
JP3189520B2
JP3189520B2 JP21175693A JP21175693A JP3189520B2 JP 3189520 B2 JP3189520 B2 JP 3189520B2 JP 21175693 A JP21175693 A JP 21175693A JP 21175693 A JP21175693 A JP 21175693A JP 3189520 B2 JP3189520 B2 JP 3189520B2
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JP
Japan
Prior art keywords
polymaleimide
solvent
purity
reaction
weight
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
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JP21175693A
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Japanese (ja)
Other versions
JPH0761969A (en
Inventor
毅 中藤
吉信 大沼
美保子 古館
薫 金山
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Mitsubishi Chemical Corp
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Mitsubishi Chemical Corp
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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、無水酢酸の存在下でポ
リマレアミド酸を脱水閉環反応させて得られるポリマレ
イミドの精製方法、換言すれば、同法により、純度の高
いポリマレイミドを簡易に製造する方法に関する。本発
明の方法で得られるポリマレイミドは、積層材料、封止
材料、電気絶縁材料、導電性ペースト、接着剤及び構造
材料として有用なものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for purifying a polymaleimide obtained by subjecting a polymaleamic acid to a dehydration and ring-closure reaction in the presence of acetic anhydride, in other words, a method for easily producing a high-purity polymaleimide by the same method. On how to do it. The polymaleimide 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、ポリアミンと無水マレイン酸との
付加反応により生成したポリマレアミド酸を脱水閉環反
応させるポリマレイミドの製造方法としては、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(特公昭59−52660号、特開昭63
−66164号公報等)が知られている。
2. Description of the Related Art Conventionally, a polymaleimide produced by an addition reaction of a polyamine with maleic anhydride is subjected to a dehydration and ring-closing reaction. A polymaleimide is produced by a ketone solvent such as acetone or a polar solvent such as N, N-dimethylformamide. , A base such as triethylamine and a metal compound are added to a dehydrating ring-closing reaction using a dehydrating agent such as acetic anhydride (JP-B-59-52660;
-66164).

【0003】[0003]

【発明が解決しようとする課題】しかし、前記の無水酢
酸を脱水剤として用いる方法では閉環反応が十分進行せ
ず、製造されたポリマレイミドは未閉環のマレアミド酸
がかなり存在する。従って、積層材料、封止材料、電気
絶縁材料、導電性ペースト等の用途には吸湿による耐
熱、強度の低下や、絶縁不良の発生等の点で好ましくな
い。また、副生する酢酸を完全に除くには煩雑な工程を
要し、同法による純度の高いポリマレイミドを簡易に製
造する方法が求められている。
However, in the above-mentioned method using acetic anhydride as a dehydrating agent, the ring-closure reaction does not proceed sufficiently, and the produced polymaleimide contains a considerable amount of unring-closed maleamic acid. Therefore, it is not preferable for applications such as a laminated material, a sealing material, an electric insulating material, and a conductive paste in terms of heat resistance due to moisture absorption, a decrease in strength, and occurrence of defective insulation. Further, a complicated process is required to completely remove acetic acid as a by-product, and there is a need for a method for easily producing high-purity polymaleimide by the same method.

【0004】[0004]

【課題を解決するための手段】本発明は、ポリアミンと
無水マレイン酸とを付加反応させて生成するポリマレア
ミド酸を無水酢酸の存在下で脱水閉環反応させて得られ
るポリマレイミドを、非水溶性有機溶媒と非プロトン性
極性溶媒の混合溶媒に溶解し、該溶液をアルカリ水溶液
で洗浄した後、ポリマレイミドを析出させることを特徴
とする、未閉環のマレアミド酸及び副生する酢酸が除か
れた純度の高いポリ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。
SUMMARY OF THE INVENTION The present invention provides a polymaleimide obtained by subjecting a polymaleamic acid produced by an addition reaction of a polyamine and maleic anhydride to a dehydration ring-closing reaction in the presence of acetic anhydride to obtain a polymaleimide obtained by adding a water-insoluble organic Dissolved in a mixed solvent of a solvent and an aprotic polar solvent, washed the solution with an aqueous alkali solution, and then precipitated polymaleimide, the purity of unringed maleamic acid and acetic acid by-produced were removed To provide a method for easily producing a polymaleimide having a high level.

【0005】(ポリマレイミド)本発明に用いられるポ
リマレイミドは、公知の方法、即ち、ポリアミンと無水
マレイン酸とをアルキルケトン等の溶媒中で付加反応さ
せ、生成するポリマレアミド酸を単離することなく脱水
剤として無水酢酸を加えて脱水閉環反応させる方法で得
られるポリマレイミドである。
(Polymaleimide) The polymaleimide used in the present invention can be prepared by a known method, that is, by subjecting a polyamine and maleic anhydride to an addition reaction in a solvent such as an alkyl ketone, without isolating the resulting polymaleamic acid. A polymaleimide obtained by a method in which acetic anhydride is added as a dehydrating agent to cause a dehydration ring-closing reaction.

【0006】(ポリアミン)ポリマレイミドの製造に用
いられるポリアミンとしては、分子内にアミノ基を2個
以上含有する化合物、例えば、m−フェニレンジアミ
ン、p−フェニレンジアミン、4,4′−ジアミノジシ
クロヘキシルメタン、1,4−ジアミノシクロヘキサン
2,6−ジアミノピリジン、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エーテル、
4,4′−ジアミノジフェニルスルファイド、4,4′
−ジアミノジフェニルスルホン、ビス−(4−アミノフ
ェニル)ジフェニルシラン、1,5−ジアミノナフタレ
ン、2,2′−ビス〔4−(4−アミノフェノキシ)フ
ェニル〕プロパン、1,1′−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〕エーテル、ビス〔4−(4
−アミノフェノキシ)フェニル〕スルホン、エチレンジ
アミン、ヘキサメチレンジアミン、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、アニリンあるいはトルイ
ジン類とホルムアルデヒドより得られる重合体、アニリ
ンあるいはトルイジン類とテレフタルアルデヒドより得
られる重合体等が挙げられる。無水マレイン酸とポリア
ミンの割合は、ポリアミンの全アミノ基1当量に対し無
水マレイン酸を0.8〜2.0、好ましくは1.0〜
1.3モル用いる。
(Polyamine) Examples of the polyamine used in the production of polymaleimide include compounds containing two or more amino groups in the molecule, for example, m-phenylenediamine, p-phenylenediamine, 4,4'-diaminodicyclohexylmethane. 1,4-diaminocyclohexane 2,6-diaminopyridine, 4,4'-diaminodiphenylmethane, 4,4'-diaminodiphenyl ether,
4,4'-diaminodiphenyl sulfide, 4,4 '
-Diaminodiphenylsulfone, bis- (4-aminophenyl) diphenylsilane, 1,5-diaminonaphthalene, 2,2'-bis [4- (4-aminophenoxy) phenyl] propane, 1,1'-bis [4 -(4-aminophenoxy) phenyl] propane, bis [4- (4-aminophenoxy) phenyl] ether, bis [4- (4
-Aminophenoxy) phenyl] sulfone, ethylenediamine, hexamethylenediamine, 3,9-bis (3-
(Aminopropyl) -2,4,8,10-tetraoxaspiro [5,5] -undecane, polymers obtained from aniline or toluidines and formaldehyde, polymers obtained from aniline or toluidines and terephthalaldehyde, and the like. Can be The ratio of maleic anhydride and polyamine is such that maleic anhydride is used in an amount of from 0.8 to 2.0, preferably from 1.0 to 2.0, per equivalent of all amino groups of the polyamine.
Use 1.3 moles.

【0007】(反応溶媒)反応溶媒としては、例えば、
アセトン、メチルエチルケトン、メチルイソプロピルケ
トン、メチルイソブチルケトン等のアルキルケトン溶媒
や、N,N−ジメチルホルムアミド、N,N−ジメチル
アセトアミド、ジメチルスルホキシド、N−メチルピロ
リドン等の極性溶媒が用いられる。溶媒量は、通常、ポ
リアミン1重量部に対して、3〜7重量部、好ましくは
4〜6重量部用いられる。
(Reaction solvent) As the reaction solvent, for example,
An alkyl ketone solvent such as acetone, methyl ethyl ketone, methyl isopropyl ketone, and methyl isobutyl ketone, and a polar solvent such as N, N-dimethylformamide, N, N-dimethylacetamide, dimethyl sulfoxide, and N-methylpyrrolidone are used. The amount of the solvent is usually 3 to 7 parts by weight, preferably 4 to 6 parts by weight based on 1 part by weight of the polyamine.

【0008】(付加反応)無水マレイン酸とポリアミン
の付加反応によるポリマレアミド酸の生成反応は一般
に、無水マレイン酸の上記溶媒溶液に所定量のポリアミ
ンを添加し20〜40℃で1〜2時間攪拌することによ
り行われる。
(Addition reaction) The polymaleamic acid formation reaction by the addition reaction of maleic anhydride and polyamine is generally performed by adding a predetermined amount of polyamine to the above-mentioned solvent solution of maleic anhydride and stirring at 20 to 40 ° C for 1 to 2 hours. This is done by:

【0009】(脱水閉環反応)ポリマレアミド酸の脱水
閉環反応は、付加反応により得られたポリマレアミド酸
を含む反応溶液に、無水酢酸、トリエチルアミン等の第
3アミン及び酢酸ニッケル等の可溶性金属塩を添加し
て、20〜100℃、好ましくは40〜70℃の範囲
で、反応系が液相を保つ圧力下で行われる。
(Dehydration Ring Closure Reaction) In the dehydration ring closure reaction of polymaleamic acid, a tertiary amine such as acetic anhydride and triethylamine and a soluble metal salt such as nickel acetate are added to a reaction solution containing polymaleamic acid obtained by the addition reaction. The reaction is carried out at a temperature of 20 to 100 ° C., preferably 40 to 70 ° C., under a pressure at which the reaction system maintains a liquid phase.

【0010】無水酢酸の量は、マレアミド酸基1当量当
たり1〜5モル、好ましくは1.1〜2.2モル用い
る。添加する第3アミンは、マレアミド酸基1当量当た
り、0.01〜2.0モル、好ましくは0.1〜0.5
モルの範囲で、可溶性金属塩は、0.001〜0.02
モル、好ましくは0.001〜0.01モルの範囲であ
る。
The amount of acetic anhydride is 1 to 5 mol, preferably 1.1 to 2.2 mol, per equivalent of maleamic acid group. The tertiary amine to be added is 0.01 to 2.0 mol, preferably 0.1 to 0.5 mol per equivalent of maleamic acid group.
In the molar range, the soluble metal salt is from 0.001 to 0.02
Mole, preferably in the range of 0.001 to 0.01 mole.

【0011】本発明の方法に用いるポリマレイミドは、
上記のようにして得られた反応生成液から、水、メタノ
ール、エタノール等のポリマレイミドの貧溶媒により析
出させ、洗浄、濾過、乾燥する等により得られるもので
あり、通常、未閉環のマレアミド酸を3〜10%含む純
度75〜95%、酸価9〜30〔mg・KOH/g〕の
ものである。ポリマレイミドの融点範囲は、ポリマレイ
ミドの種類によって異なるが、通常、60〜160℃で
幅広い融点を示す。
The polymaleimide used in the method of the present invention is
From the reaction product liquid obtained as above, water, methanol, precipitated by a poor solvent of polymaleimide such as ethanol, washed, filtered, obtained by drying, etc., usually, unringed maleamic acid Is 3 to 10%, the purity is 75 to 95%, and the acid value is 9 to 30 [mg · KOH / g]. The melting point range of the polymaleimide varies depending on the type of the polymaleimide, but generally shows a wide melting point at 60 to 160 ° C.

【0012】(混合溶媒)本発明の方法では、上記のよ
うにして得られたポリマレイミドを、非水溶性有機溶媒
と非プロトン性極性溶媒の混合溶媒に溶解させる。非水
溶性有機溶媒は、ポリマレイミドを完全に溶解させるこ
との出来る溶媒であり、具体的には、(1)ベンゼン、
トルエン、キシレン、エチルベンゼン、ジエチルベンゼ
ン、ブチルベンゼン、キュメン、メシチレン等の芳香族
炭化水素類、(2)クロロホルム、ジクロルエタン、ト
リクロロエチレン、1,2−ジクロルプロパン、クロル
ベンゼン、ジクロルベンゼン、クロルトルエン、トリク
ロルエタン、1,1,2,2−テトラクロルエタン等の
ハロゲン化炭化水素類、(3)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エステル類が挙げられる。
(Mixed solvent) In the method of the present invention, the polymaleimide obtained as described above is dissolved in a mixed solvent of a water-insoluble organic solvent and an aprotic polar solvent. The water-insoluble organic solvent is a solvent capable of completely dissolving the polymaleimide, and specifically, (1) benzene,
Aromatic hydrocarbons such as toluene, xylene, ethylbenzene, diethylbenzene, butylbenzene, cumene, mesitylene, (2) chloroform, dichloroethane, trichloroethylene, 1,2-dichloropropane, chlorobenzene, dichlorobenzene, chlorotoluene, trichloro Halogenated hydrocarbons such as ethane, 1,1,2,2-tetrachloroethane, (3) ethyl formate, n-butyl formate, ethyl acetate, propyl acetate, n-butyl acetate, isobutyl acetate, sec-hexyl acetate And esters such as 2-ethylhexyl acetate, ethyl propionate, n-butyl propionate, and ethyl isovalerate.

【0013】非プロトン性極性溶媒としては、ポリマレ
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、テトラメチル尿素酸等のアミド系溶媒、
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、中でも、
アミド系溶媒が好ましく用いられる。
As the aprotic polar solvent, a solvent which easily dissolves polymaleamic acid, for example, N, N-dimethylformamide, N, N-dimethylacetamide, N-
Amide solvents such as methyl-2-pyrrolidone, 1,3-dimethyl-2-imidazolidinone, tetramethylurea acid,
Sulfur-based solvents such as dimethyl sulfoxide, phosphorus-based solvents such as hexamethylphosphoramide, and the like.
Amide solvents are preferably used.

【0014】混合溶媒中の非プロトン性極性溶媒の量
は、0.1〜30重量%、好ましくは1〜20重量%で
ある。非水溶性有機溶媒は、ポリマレイミド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。ポリマレイミドの溶解は、通常、20〜
95℃の範囲で、均一溶液になるまで加温して溶解させ
る。
The amount of the aprotic polar solvent in the mixed solvent is 0.1 to 30% by weight, preferably 1 to 20% by weight. The water-insoluble organic solvent is used in a proportion of 1 to 50 parts by weight, preferably 2 to 20 parts by weight, based on 1 part by weight of the polymaleimide. The dissolution of polymaleimide is usually 20 to
Heat and dissolve in a range of 95 ° C. until a homogeneous solution is obtained.

【0015】(アルカリ水溶液)本発明において使用す
るアルカリ水溶液としては、各種塩基性物質の水溶液を
用いることができるが、洗浄性、操作性、経済性などか
らまた、残存イオンの問題からアンモニア水溶液が好ま
しい。アルカリ水溶液の濃度は、1〜20重量%、好ま
しくは5〜10重量%の範囲のものがよい。アルカリ水
溶液の量は、特に制限はないが、混合有機溶媒の0.1
〜1重量部程度用いるのが好ましい。
(Aqueous Alkaline Solution) As the alkaline aqueous solution used in the present invention, aqueous solutions of various basic substances can be used. However, an aqueous ammonia solution is used from the viewpoints of detergency, operability, economy, etc. preferable. The concentration of the aqueous alkali solution is in the range of 1 to 20% by weight, preferably 5 to 10% by weight. The amount of the aqueous alkali solution is not particularly limited, but may be 0.1% of the mixed organic solvent.
It is preferable to use about 1 part by weight.

【0016】(洗浄)洗浄は、前記ポリマレイミドの混
合有機溶媒溶液に、前記アルカリ水溶液を加えて、攪拌
後、静置し、油水分離して行う。攪拌は、一般に、回転
数30〜300rpmで、3〜30分間攪拌することに
より行われる。洗浄は、20〜95℃の温度範囲で、1
〜5回行う。
(Washing) Washing is carried out by adding the aqueous alkali solution to the mixed organic solvent solution of the polymaleimide, stirring, and then allowing to stand, followed by oil-water separation. Stirring is generally performed by stirring at a rotation speed of 30 to 300 rpm for 3 to 30 minutes. Washing is carried out in a temperature range of 20 to 95 ° C.
Perform ~ 5 times.

【0017】洗浄後、1回以上水洗を行うと、より高純
度のポリマレイミドが得られる。得られた有機層から高
純度のポリマレイミドを得るには、溶媒を留去した後、
溶融抜き出し又は析出させる方法がある。溶媒の留去
は、溶媒の蒸発温度以上で、通常、40〜200℃、圧
力760〜0.1mmHgの範囲である。
After the washing, washing with water at least once gives a higher purity polymaleimide. To obtain a high-purity polymaleimide from the obtained organic layer, after distilling off the solvent,
There is a method of extracting or melting. The solvent is distilled off at a temperature equal to or higher than the evaporation temperature of the solvent, usually at 40 to 200 ° C. and at a pressure of 760 to 0.1 mmHg.

【0018】溶融抜き出しの場合は、最終的にはポリマ
レイミドの融点以上まで昇温し、実質的に溶媒が無くな
るまで、具体的には溶媒残存量が2重量%以下となるま
で留去して、マレイミドを溶融状態で抜き出す。
In the case of melt extraction, the temperature is finally raised to the melting point of the polymaleimide or higher, and the solvent is distilled off until the solvent is substantially eliminated, specifically, until the residual amount of the solvent becomes 2% by weight or less. Then, the maleimide is extracted in a molten state.

【0019】また、析出させる場合は、通常、溶媒の一
部、仕込み量の20〜95重量%に相当する量を留去し
た後、水、メタノール、エタノール等のポリマレイミド
に対する貧溶媒をポリマレイミド1重量部に対して1〜
30重量部、好ましくは2〜15重量部添加して、ポリ
マレイミドを析出させ、濾別、乾燥して結晶状態で取り
出す。
In the case of precipitation, usually, after distilling off a part of the solvent, an amount corresponding to 20 to 95% by weight of the charged amount, a poor solvent for the polymaleimide such as water, methanol and ethanol is removed. 1 to 1 part by weight
The polymaleimide is precipitated by adding 30 parts by weight, preferably 2 to 15 parts by weight, separated by filtration, dried and taken out in a crystalline state.

【0020】得られるポリマレイミドは、通常、純度9
0%以上、酸価0.1〜5〔mg・KOH/g〕の高純
度のものである。
The resulting polymaleimide generally has a purity of 9%.
It has a high purity of 0% or more and an acid value of 0.1 to 5 [mg · KOH / g].

【0021】[0021]

【実施例】以下、実施例により本発明をより具体的に説
明する。尚、ポリマレイミドの融点はキャピラリー法、
純度は液体クロマトグラフ(示差屈折率検出器)の面積
百分率、酸価はN/10KOHエタノール溶液で滴定に
より測定した。
The present invention will be described more specifically with reference to the following examples. The melting point of polymaleimide is determined by the capillary method.
The purity was measured by liquid chromatograph (differential refractive index detector) area percentage, and the acid value was measured by titration with an N / 10 KOH ethanol solution.

【0022】参考例1 還流冷却器、温度計、滴下ロートおよび攪拌機を付した
300mlの四口フラスコに、無水マレイン酸21.6
g、アセトン13.2gを入れ攪拌溶解した。4,4′
−ジアミノジフェニルメタン19.8gをアセトン6
9.3gに溶解し20〜40℃に保持した上記フラスコ
内に2時間かけて滴下した後、同温度で1時間攪拌し
た。次いで酢酸ニッケル0.2g、トリエチルアミン5
g、無水酢酸25.5gを加えて65℃で2時間反応さ
せた。
Reference Example 1 Maleic anhydride (21.6) was placed in a 300 ml four-necked flask equipped with a reflux condenser, a thermometer, a dropping funnel and a stirrer.
g and 13.2 g of acetone were dissolved by stirring. 4,4 '
19.8 g of diaminodiphenylmethane in acetone 6
After dissolving in 9.3 g and dripping into the flask maintained at 20 to 40 ° C. over 2 hours, the mixture was stirred at the same temperature for 1 hour. Next, 0.2 g of nickel acetate and triethylamine 5
g and acetic anhydride 25.5 g were added and reacted at 65 ° C. for 2 hours.

【0023】室温まで冷却させた後、500mlの水中
に滴下して黄色のN,N′−(4,4′−ジフェニルメ
タン)ビスマレイミド32.2gを得た(収率93
%)。このマレイミドは融点144〜151℃、純度8
9%、酸価9.1mg・KOH/gであった。
After cooling to room temperature, the mixture was dropped into 500 ml of water to obtain 32.2 g of yellow N, N '-(4,4'-diphenylmethane) bismaleimide (yield: 93).
%). This maleimide has a melting point of 144 to 151 ° C and a purity of 8
It was 9% and the acid value was 9.1 mg · KOH / g.

【0024】参考例2 参考例1において、ポリアミンとして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〕−ウンデカンを用い、アセトンの量を
2倍とした以外は参考例1と同様にしてポリマレイミド
を得た。
Reference Example 2 In Reference Example 1, 3,9-bis (3
-Aminopropyl) -2,4,8,10-tetraoxaspiro [5,5] -undecane, and a polymaleimide was obtained in the same manner as in Reference Example 1 except that the amount of acetone was doubled.

【0025】参考例3〜5 参考例1において、ポリアミンを表1のように変えた以
外は参考例1と同様にしてポリマレイミドを得た。参考
例2〜5で得られたポリマレイミドの性状を表1に示
す。
Reference Examples 3 to 5 Polymaleimides were obtained in the same manner as in Reference Example 1, except that the polyamine was changed as shown in Table 1. Table 1 shows the properties of the polymaleimides obtained in Reference Examples 2 to 5.

【0026】[0026]

【表1】 [Table 1]

【0027】実施例1 冷却器、温度計および攪拌機を備えた300mlの四口
フラスコ内に、参考例1で得たビスマレイミド20g、
クロルベンゼン80gおよび、N−メチル−2−ピロリ
ドン1gを仕込み内温を80℃に調整しながら攪拌溶解
させた。溶解後、フラスコ内に5%アンモニア水溶液4
0gを加え、5分間攪拌し、2分間静置後油水分離し
た。さらに純水40gを加えて同様にして洗浄した。
Example 1 In a 300 ml four-necked flask equipped with a condenser, a thermometer and a stirrer, 20 g of the bismaleimide obtained in Reference Example 1 was added.
80 g of chlorobenzene and 1 g of N-methyl-2-pyrrolidone were charged and dissolved by stirring while adjusting the internal temperature to 80 ° C. After dissolution, 5% aqueous ammonia 4
After adding 0 g, the mixture was stirred for 5 minutes, left standing for 2 minutes, and then separated into oil and water. Further, 40 g of pure water was added, and washing was performed in the same manner.

【0028】次いで、油水分離した有機層から、温度8
0℃に保持した油浴中、減圧下(100〜20mmH
g)でクロルベンゼンを40g留去した(留去率50重
量%)。溶液を40℃まで冷却後、メタノール120g
を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18.5gを得た。(収率
92.5%) このビスマレイミドは、融点151〜152℃、純度9
2.2%、酸価1.3(mg・KOH/g)であった。
Next, the organic layer separated from oil and water was heated to a temperature of 8 ° C.
In an oil bath maintained at 0 ° C., under reduced pressure (100-20 mmH
In g), 40 g of chlorobenzene was distilled off (distillation rate: 50% by weight). After cooling the solution to 40 ° C.,
Was added to obtain a slurry liquid. This is filtered off, dried and
18.5 g of pale yellow bismaleimide powder was obtained. (Yield 92.5%) This bismaleimide has a melting point of 151 to 152 ° C and a purity of 9%.
The acid value was 2.2% and the acid value was 1.3 (mg · KOH / g).

【0029】実施例2〜5 実施例1において、参考例2〜5で得られたポリマレイ
ミドを用い、非水溶性有機溶媒として表2に示す溶媒を
用いた他は実施例1と同様にしてポリマレイミドを得
た。得られたポリマレイミドの性状を表2に示す。
Examples 2 to 5 In the same manner as in Example 1 except that the polymaleimide obtained in Reference Examples 2 to 5 was used and the solvents shown in Table 2 were used as the water-insoluble organic solvents. A polymaleimide was obtained. Table 2 shows the properties of the obtained polymaleimide.

【0030】[0030]

【表2】 [Table 2]

【0031】実施例6 実施例4において、洗浄後の有機層を温度110℃に保
持した油浴中、常圧下で1.2−ジクロロエタンの留去
を行い、流出が少なくなったところで減圧(10mmH
g)にして、完全に流出しなくなるまで保持した後、淡
黄色のポリマレイミドを溶融状態で抜き出した他は、実
施例4と同様に行った。得られたポリマレイミド18.
8g(収率94.0%)は、融点60〜69℃、酸価
2.8(mg・KOH/g)であった。
Example 6 In Example 4, 1.2-dichloroethane was distilled off under normal pressure in an oil bath in which the washed organic layer was kept at 110 ° C., and when the outflow was reduced, the pressure was reduced (10 mmH).
g), and the procedure was carried out in the same manner as in Example 4 except that the pale yellow polymaleimide was taken out in a molten state after it was held until it did not completely flow out. 18. Polymaleimide obtained
8 g (94.0% yield) had a melting point of 60 to 69 ° C and an acid value of 2.8 (mg KOH / g).

【0032】比較例1 実施例5において、5%アンモニア水溶液を用いず、か
わりに、純水40gで2回洗浄した他は、実施例5と同
様にして淡黄色のビスマレイミド粉末17.2gを得
た。(収率86%) このビスマレイミドは、融点51〜68℃、酸価8.0
(mg・KOH/g)であった。
Comparative Example 1 17.2 g of a pale yellow bismaleimide powder was prepared in the same manner as in Example 5 except that washing was performed twice with 40 g of pure water instead of using a 5% aqueous ammonia solution. Obtained. (Yield 86%) This bismaleimide has a melting point of 51 to 68 ° C. and an acid value of 8.0.
(Mg · KOH / g).

【0033】比較例2 実施例4において、溶媒として、クロルベンゼン80g
のみを仕込んだ他は、実施例4と同様にしてポリ(フェ
ニルメチレン)マレイミドを溶解させた。溶解後、5%
アンモニア水溶液40gで実施例5と同様にして洗浄し
たところ黒色のタールを生成した。
Comparative Example 2 In Example 4, 80 g of chlorobenzene was used as a solvent.
Poly (phenylmethylene) maleimide was dissolved in the same manner as in Example 4 except that only was charged. 5% after dissolution
When washed with 40 g of an aqueous ammonia solution in the same manner as in Example 5, a black tar was produced.

フロントページの続き (72)発明者 金山 薫 茨城県稲敷郡阿見町中央8丁目3番1号 三菱油化株式会社筑波総合研究所内 (56)参考文献 特開 平5−140097(JP,A) (58)調査した分野(Int.Cl.7,DB名) C07D 207/452 C08F 22/40 CA(STN) REGISTRY(STN)Continued on the front page (72) Inventor Kaoru Kanayama 8-3-1 Chuo, Ami-cho, Inashiki-gun, Ibaraki Pref. Tsukuba Research Laboratory, Mitsubishi Yuka Co., Ltd. (56) References JP-A-5-140097 (JP, A) ( 58) Field surveyed (Int.Cl. 7 , DB name) C07D 207/452 C08F 22/40 CA (STN) REGISTRY (STN)

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ポリアミンと無水マレイン酸との付加反
応により生成するポリマレアミド酸を無水酢酸の存在下
で脱水閉環反応させて得られるポリマレイミドを、非水
溶性有機溶媒と非プロトン性極性溶媒の混合溶媒に溶解
してアルカリ水溶液で洗浄することを特徴とする高純度
ポリマレイミドの製造方法。
1. A polymaleimide obtained by subjecting a polymaleamic acid formed by an addition reaction between a polyamine and maleic anhydride to a dehydration ring-closing reaction in the presence of acetic anhydride to obtain a mixture of a water-insoluble organic solvent and an aprotic polar solvent. A method for producing a high-purity polymaleimide, comprising dissolving in a solvent and washing with an aqueous alkaline solution.
JP21175693A 1993-08-26 1993-08-26 Method for producing high-purity polymaleimide Expired - Fee Related JP3189520B2 (en)

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JPH1051136A (en) * 1996-05-28 1998-02-20 Mitsui Petrochem Ind Ltd Manufacture of printed-wiring board
ES2215860T3 (en) 2000-10-19 2004-10-16 Bridgestone Corporation A BLEND OF RUBBER AND OTHER MISCELLANEOUS INGREDIENTS CONTAINING POLIMALEIMIDE AND A COVER.
JP2002199877A (en) * 2000-11-30 2002-07-16 Advanced Biotechnologies Ltd Method for reversible inactivation of enzyme and kit containing the enzyme
CN104140176B (en) * 2013-09-16 2016-03-23 河南省华鼎高分子合成树脂有限公司 The treatment process of the rectifying waste liquid of output in a kind of maleimide production process
JP6764470B2 (en) * 2016-03-29 2020-09-30 日本化薬株式会社 Maleimide resin, curable resin composition and cured product thereof
US20180201579A1 (en) * 2017-01-17 2018-07-19 Unitika Ltd. Bismaleimide and production method thereof
JP7099700B2 (en) * 2017-06-19 2022-07-12 ユニチカ株式会社 Bismaleimide modified product and its manufacturing method
JP2019189595A (en) * 2018-04-24 2019-10-31 ユニチカ株式会社 Bismaleimide solution, and carbodiimide-modified bismaleimide
JP6555792B1 (en) 2018-05-10 2019-08-07 ユニチカ株式会社 Method for producing maleimide
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