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JPS5829791B2 - Maleimidonoseizouhou - Google Patents
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JPS5829791B2 - Maleimidonoseizouhou - Google Patents

Maleimidonoseizouhou

Info

Publication number
JPS5829791B2
JPS5829791B2 JP50013993A JP1399375A JPS5829791B2 JP S5829791 B2 JPS5829791 B2 JP S5829791B2 JP 50013993 A JP50013993 A JP 50013993A JP 1399375 A JP1399375 A JP 1399375A JP S5829791 B2 JPS5829791 B2 JP S5829791B2
Authority
JP
Japan
Prior art keywords
maleimide
reaction
acid
producing
solvent
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
JP50013993A
Other languages
Japanese (ja)
Other versions
JPS5188959A (en
Inventor
詔夫 高谷
浩 小池
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.)
Nippon Shokubai Co Ltd
Original Assignee
Nippon Shokubai 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 Nippon Shokubai Co Ltd filed Critical Nippon Shokubai Co Ltd
Priority to JP50013993A priority Critical patent/JPS5829791B2/en
Publication of JPS5188959A publication Critical patent/JPS5188959A/ja
Publication of JPS5829791B2 publication Critical patent/JPS5829791B2/en
Expired 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

Landscapes

  • Pyrrole Compounds (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Description

【発明の詳細な説明】 本発明はマレイミドの製造法に関するものである。[Detailed description of the invention] The present invention relates to a method for producing maleimide.

詳しく述べれば本発明はN−カルバモイルマレアミン酸
からマレイミドを製造するものであって、更に詳しくは
N−カルバモイルマレアミン酸を溶媒中で触媒の存在下
50〜150℃の温度に維持してマレイミドに変換せし
めることを特徴とするマレイミドの製造法に関するもの
である。
More specifically, the present invention is directed to producing maleimide from N-carbamoyl maleamic acid, and more specifically, by maintaining N-carbamoyl maleamic acid in a solvent at a temperature of 50 to 150°C in the presence of a catalyst to form maleimide. The present invention relates to a method for producing maleimide, which is characterized by converting maleimide into

マレイミドは各種高分子化合物の原料として、また殺菌
剤、殺虫剤、除草剤、抗酸化剤、ゴムの硬化剤、防蝕剤
等の原料としてその利用範囲は極めて広い化合物である
にもかかわらず工業的に有利な製造法は末だ確立されて
いない。
Maleimide is a compound that has an extremely wide range of uses as a raw material for various polymeric compounds, and as a raw material for fungicides, insecticides, herbicides, antioxidants, rubber hardening agents, anticorrosion agents, etc., but it is not used industrially. An advantageous manufacturing method has yet to be established.

マレイミドの製造法としては従来、無水マレイン酸にフ
ラン又はシクロペンタジェンを反応させてテイールス・
アルタ−付加物を生ぜしめ、次いでこれをアンモニアで
処理してマレイミド付加物に変換し、得られたマレイミ
ド付加物を熱分解してマレイミドを生ぜしめ、これを分
離取得する方法が古くから知られているが、工程が複雑
で工業的な方法とはいえない。
Conventionally, maleimide has been produced by reacting maleic anhydride with furan or cyclopentadiene.
A long-known method has been known in which an alter-adduct is produced, which is then treated with ammonia to convert it into a maleimide adduct, and the resulting maleimide adduct is thermally decomposed to produce maleimide, which is then separated and obtained. However, the process is complicated and cannot be called an industrial method.

また米国特許第2788349号明細書はNカルバモイ
ルマレアミン酸を原料として式(lX2)に示す様な反
応によってマレイミドを製造する方法を開示している。
Further, US Pat. No. 2,788,349 discloses a method for producing maleimide using N-carbamoyl maleamic acid as a raw material through a reaction as shown in formula (1X2).

この方法は反応式からも明らかな様に原料のN−カルバ
モイルマレアミン酸からますN−カルバモイルマレイミ
ドを製造単離し、かくして得られたN−カルバモイルマ
レイミドを単に加熱分解するか又は塩化亜鉛を触媒とし
て加熱分解するか又はジメチルホルムアミドを溶媒かつ
触媒として使用し95〜1000Cで分解してマレイミ
ドを製造する方法であり中間体であるN−カルバモイル
マレイミドの製造及び単離を行なうことが必須条件とな
っている。
As is clear from the reaction formula, this method involves producing and isolating N-carbamoylmaleimide from the raw material N-carbamoylmaleamic acid, and then simply thermally decomposing the N-carbamoylmaleimide or using zinc chloride as a catalyst. This is a method of producing maleimide by thermal decomposition or decomposition at 95 to 1000 C using dimethylformamide as a solvent and catalyst, and it is an essential condition to produce and isolate the intermediate N-carbamoylmaleimide. There is.

しかしながらN−カルバモイルマレイミドを製造するた
めには原料のN−カルバモイルマレアミン酸と当モルの
酸無水物とから脱水閉環反応を行なわしめる事を必要と
し、その際酸無水物が水和されて消費されN−カルバモ
イルマレアミン酸からマレイミドを製造する方法として
は単に工程が複雑であると云うのみならず副原料費の負
担が大きく工業的製造法であるとはいい難い。
However, in order to produce N-carbamoylmaleimide, it is necessary to carry out a dehydration ring-closing reaction from the raw material N-carbamoylmaleamic acid and an equimolar amount of acid anhydride, during which the acid anhydride is hydrated and consumed. However, the process for producing maleimide from N-carbamoylmaleamic acid is not only complicated, but also requires a large cost of auxiliary raw materials, so it cannot be said to be an industrial production method.

本発明の目的は工業的に実施可能なマレイミドの製造法
を提供することにあり、詳しくはN−カルバモイルマレ
アミン酸を原料として何らの中間体も単離することなく
一工程でマレイミドを製造する方法を提供することにあ
る。
The purpose of the present invention is to provide an industrially implementable method for producing maleimide, and more specifically, maleimide is produced in one step using N-carbamoylmaleamic acid as a raw material without isolating any intermediates. The purpose is to provide a method.

本発明者らは上記目的のために種々研究の結果N−カル
バモイルマレアミン酸を不活性溶媒中で銅、亜鉛、ニッ
ケル又はコバルトから選ばれた少くとも一種の金属化合
物の触媒の存在下50〜150℃の温度に維持すること
によりマレイミドを生ずることを見出し本発明を完成し
た。
As a result of various studies for the above purpose, the present inventors prepared N-carbamoyl maleamic acid in an inert solvent in the presence of a catalyst of at least one metal compound selected from copper, zinc, nickel or cobalt for 50 to 50 minutes. The present invention was completed by discovering that maleimide can be produced by maintaining the temperature at 150°C.

本発明の出発原料であるN−カルバモイルマレアミン酸
は公知の方法、例えば無水マレイン酸と尿素との反応に
より極めて容易に且つ高収率、高純度で得られるので目
的とするマレイミドの製造用原料としては好適である。
N-carbamoylmaleamic acid, which is the starting material of the present invention, can be obtained extremely easily, in high yield, and with high purity by a known method, for example, by the reaction of maleic anhydride with urea, so it can be used as a raw material for producing the target maleimide. It is suitable as

しかし本発明が出発原料とするN−カルバモイルマレア
ミン酸の製造方法には例ら制限されないのはいうまでも
ない。
However, it goes without saying that the present invention is not limited to the method for producing N-carbamoylmaleamic acid as a starting material.

本発明の方法によれば酸無水物の如き副原料を必要とし
ないで一工程でマレイミドを完成せしめることができる
ので公知方法に比べて工程も簡素で極めて経済的である
According to the method of the present invention, maleimide can be completed in one step without the need for auxiliary raw materials such as acid anhydrides, so the process is simpler and extremely economical compared to known methods.

本発明の方法は次の様にして実施される。The method of the present invention is carried out as follows.

N−カルバモイルマレアミン酸と銅、亜鉛、ニッケル又
はコバルトから選ばれた少くとも一種の金属化合物の触
媒を溶媒中に加えて溶解または一部懸濁せしめ、この混
合液を所定の温度に維持し所定の反応時間の後にマレイ
ミドを含有する反応液を得る。
A catalyst consisting of N-carbamoyl maleamic acid and at least one metal compound selected from copper, zinc, nickel, or cobalt is added to a solvent to dissolve or partially suspend the mixture, and the mixture is maintained at a predetermined temperature. After a predetermined reaction time, a reaction solution containing maleimide is obtained.

反応液からのマレイミドの取得は常法により行ない得る
Maleimide can be obtained from the reaction solution by a conventional method.

本発明において触媒として用いられる金属化合物は銅、
亜鉛、ニッケル又はコバルトの化合物であり、化合物の
態様は特に限定されるものではないが好適なものとして
塩化物、酸化物または酢酸塩が挙げられる。
The metal compounds used as catalysts in the present invention include copper,
It is a compound of zinc, nickel or cobalt, and the form of the compound is not particularly limited, but preferred examples include chloride, oxide or acetate.

触媒の使用量は原料のN−カルバモイルマレアミン酸に
対し1モルφ以上、好ましくは5〜100モル係であり
、1モルφ以下の使用量ではその効果は認め難い。
The amount of the catalyst to be used is 1 mol φ or more, preferably 5 to 100 mol, relative to the raw material N-carbamoylmaleamic acid, and the effect is hard to be observed if the amount used is 1 mol φ or less.

本発明の方法において用いる溶媒は特に限定されるもの
ではないがN−カルバモイルマレアミン酸が可溶性であ
り且つ生成マレイミドに不活性である溶媒が好ましく、
例えばジメチルホルムアミド、ジメチルスルホキシドの
如き非プロトン性極性溶媒が特に好ましい。
The solvent used in the method of the present invention is not particularly limited, but it is preferably a solvent in which N-carbamoylmaleamic acid is soluble and inert to the maleimide produced.
For example, aprotic polar solvents such as dimethylformamide and dimethylsulfoxide are particularly preferred.

本発明の方法における反応温度は50〜150℃、好ま
しくは70〜120℃である。
The reaction temperature in the method of the invention is 50-150°C, preferably 70-120°C.

50℃以下の温度では生成速度が極めて遅いため好まし
くない。
Temperatures below 50° C. are not preferred because the production rate is extremely slow.

また生成物であるマレイミドは非常に重合しやすい物質
であるので150℃以上の反応温度は好ましくない。
Furthermore, since the maleimide product is a substance that is highly polymerizable, a reaction temperature of 150° C. or higher is not preferred.

かくして得られたマレイミドを含有する反応液からは、
容易に常法によりマレイミドを単離することができる。
From the thus obtained reaction solution containing maleimide,
Maleimide can be easily isolated by conventional methods.

すなわち反応液から溶媒を溜去した後に残渣を蒸溜する
か又は残渣から溶剤抽出を行なうことによってマレイミ
ドを得ることができる。
That is, maleimide can be obtained by distilling off the solvent from the reaction solution and then distilling the residue, or by performing solvent extraction from the residue.

以下に実施例を示し本発明を更に詳細に説明する。The present invention will be explained in more detail with reference to Examples below.

実施例 1 ジメチルホルムアミド100m1とN−カルバモイルマ
レアミン酸200g及び塩化第二銅9.Ogをフラスコ
に入れ撹拌しながら100℃に昇温後1時間反応を続け
た。
Example 1 100 ml of dimethylformamide, 200 g of N-carbamoyl maleamic acid and cupric chloride9. Og was placed in a flask, and the temperature was raised to 100° C. while stirring, and the reaction was continued for 1 hour.

反応終了後減圧下80’Cでジメチルホルムアミドを溜
去し、次にジメチルホルムアミド溜置後の残渣に酢酸エ
チル40dを加えて湯浴で30分間還流加熱した。
After the reaction was completed, dimethylformamide was distilled off at 80'C under reduced pressure, and then 40 d of ethyl acetate was added to the residue after distilling dimethylformamide, and the mixture was heated under reflux in a water bath for 30 minutes.

冷却後流過してろ液より酢酸エチルを溜置後残渣を5m
πHg、油浴温度120℃で処理したところ生成物が溜
出し空冷捕集管で7.7gの結晶を得た。
After cooling, filter the filtrate and collect ethyl acetate from the filtrate.
When treated at πHg and an oil bath temperature of 120° C., the product was distilled out and 7.7 g of crystals were obtained in an air-cooled collection tube.

得られた生成物は以下の分析の結果マレイミドであると
確認された。
The obtained product was confirmed to be maleimide as a result of the following analysis.

融点=88〜90℃、元素分析:窒素外14.39重量
咎、赤外線吸収スペクトルがマレイミドのスベクトルと
完全に一致 なお出発原料のN−カルバモイルマレアミン酸に対する
マレイミドの収率は62.7モルφであった。
Melting point = 88-90°C, elemental analysis: 14.39 weight strength (excluding nitrogen), infrared absorption spectrum completely matches the svector of maleimide, and the yield of maleimide based on the starting material N-carbamoyl maleamic acid is 62.7 mol. It was φ.

実施例 2 実施例1と同様に反応を行ない、反応終了後減圧下80
℃でジメチルホルムアミドを溜置後実施例1の溶剤によ
る抽出操作に代ってそのまま減圧蒸溜を行なった。
Example 2 A reaction was carried out in the same manner as in Example 1, and after the reaction was completed, the reaction was carried out under reduced pressure for 80 minutes.
After dimethylformamide was distilled at .degree. C., vacuum distillation was directly performed instead of the solvent extraction operation in Example 1.

即ち残渣を5mmHg、油浴温度120℃で処理した結
果マレイミドを61.0モル饅の収率で得た。
That is, as a result of treating the residue at 5 mmHg and an oil bath temperature of 120° C., maleimide was obtained in a yield of 61.0 mol.

実施例 3〜7 触媒及びその使用量を第1表に示した様に変更した以外
は実施例1と同様に行ない第1表に示した様な結果を得
た。
Examples 3 to 7 The same procedure as in Example 1 was carried out except that the catalyst and the amount used thereof were changed as shown in Table 1, and the results shown in Table 1 were obtained.

実施例 8 溶媒にジメチルスルホキシドを用いた以外は実施例1と
同様に行なった結果マレイミドを3.57モル咎の収率
で得た。
Example 8 The same procedure as in Example 1 was carried out except that dimethyl sulfoxide was used as the solvent. As a result, maleimide was obtained in a yield of 3.57 mol.

実施例 9 反応温度を110℃、反応時間を30分にした以外は実
施例1と同様に行なった結果マレイミドを60.8モル
係の収率で得た。
Example 9 The same procedure as in Example 1 was carried out except that the reaction temperature was 110° C. and the reaction time was 30 minutes. As a result, maleimide was obtained in a yield of 60.8 mol.

実施例 10 反応温度を70℃、反応時間を8時間で行ない、溶媒回
収を減圧下70℃で行なった以外は実施例1と同様に行
なった結果マレイミドを560モル係の収率で得た。
Example 10 The same procedure as in Example 1 was conducted except that the reaction temperature was 70° C., the reaction time was 8 hours, and the solvent was recovered at 70° C. under reduced pressure. As a result, maleimide was obtained in a yield of 560 mol.

Claims (1)

【特許請求の範囲】[Claims] IN−カルバモイルマレアミン酸を、銅、亜鉛、ニッケ
ル又はコバルトよりなる群から選ばれた少くとも一種の
金属化合物の存在下に、不活性な有機溶媒中50〜15
00の温度に維持してマレイミドに変換せしめることを
特徴とするマレイミドの製造法。
IN-carbamoyl maleamic acid is dissolved in an inert organic solvent in the presence of at least one metal compound selected from the group consisting of copper, zinc, nickel, or cobalt.
1. A method for producing maleimide, which comprises converting maleimide by maintaining the temperature at 0.00.
JP50013993A 1975-02-04 1975-02-04 Maleimidonoseizouhou Expired JPS5829791B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP50013993A JPS5829791B2 (en) 1975-02-04 1975-02-04 Maleimidonoseizouhou

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP50013993A JPS5829791B2 (en) 1975-02-04 1975-02-04 Maleimidonoseizouhou

Publications (2)

Publication Number Publication Date
JPS5188959A JPS5188959A (en) 1976-08-04
JPS5829791B2 true JPS5829791B2 (en) 1983-06-24

Family

ID=11848745

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50013993A Expired JPS5829791B2 (en) 1975-02-04 1975-02-04 Maleimidonoseizouhou

Country Status (1)

Country Link
JP (1) JPS5829791B2 (en)

Also Published As

Publication number Publication date
JPS5188959A (en) 1976-08-04

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