JPS5931742A - Preparation of unsaturated amide - Google Patents

Preparation of unsaturated amide

Info

Publication number
JPS5931742A
JPS5931742A JP57141875A JP14187582A JPS5931742A JP S5931742 A JPS5931742 A JP S5931742A JP 57141875 A JP57141875 A JP 57141875A JP 14187582 A JP14187582 A JP 14187582A JP S5931742 A JPS5931742 A JP S5931742A
Authority
JP
Japan
Prior art keywords
copper
copper salt
hydroborate
water
acrylonitrile
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
JP57141875A
Other languages
Japanese (ja)
Inventor
Hidefumi Hirai
平井 英史
Makoto Komiyama
真 小宮山
Hidehiko Wakabayashi
秀彦 若林
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP57141875A priority Critical patent/JPS5931742A/en
Publication of JPS5931742A publication Critical patent/JPS5931742A/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

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

PURPOSE:To improve the yield with a high activity in hydrating acrylonitrile or methacrylonitrile to give the titled compound, by using an aqueous homogeneous colloidal copper solution obtained by treating a copper salt with a hydroborate in the presence of a protective polymer. CONSTITUTION:Acrylonitrile or methacrylonitrile is reacted with water in the presence of a homogeneous colloidal copper as a catalyst to give the aimed compound. The homogeneous colloidal copper solution is synthesized by dissolving a protective polymer and a copper salt in water, and adding an aqueous solution of a hydroborate thereto. The hydroborate to be added is used in a molar amount of about 2 times of that of the copper salt. A water-soluble polymer having the protective colloid action, e.g. polyvinylpyrrolidone, is used as the protective polymer, and the residue equivalent amount thereof to be used is 5-60 times, preferably 10-40 times, of that of the copper salt. The copper salt is suitably used in an amount of about 1-30millimol based on one lwater.

Description

【発明の詳細な説明】 本発明は、不飽和アミドの製造法に関するものであり、
詳しくは、均一系金属触媒の存在下、アクリロニトリル
、または、メタクリロニトリルを接触水和することによ
って、アクリルアミド、捷たは、メタクリルアミドを製
造する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing unsaturated amides,
Specifically, the present invention relates to a method for producing acrylamide, saccharide, or methacrylamide by catalytically hydrating acrylonitrile or methacrylonitrile in the presence of a homogeneous metal catalyst.

触媒の存在下、ニトリルを接触的に水和して、対応する
アミドを製造する方法は公知であり、丑だ、アクリロニ
トリル、または、メタクリロニトリルのような不飽和ニ
トリルより対応するアミドを製造する際の触媒として、
銅塩をヒドロホウ酸塩で還元して得られる不均一系金属
銅触媒が活性を示すことも公知である。しかし実用的見
地からは、さらに高活性で高選択性の触媒の開発が望ま
れている。
Methods are known for the catalytic hydration of nitriles in the presence of catalysts to produce the corresponding amides from unsaturated nitriles such as acrylonitrile, acrylonitrile, or methacrylonitrile. As a catalyst,
It is also known that heterogeneous metallic copper catalysts obtained by reducing copper salts with hydroborates exhibit activity. However, from a practical standpoint, it is desired to develop catalysts with even higher activity and selectivity.

本発明者らは、これらの結果をふまえて、鋭意研究した
結果、銅塩を適当な保護ポリマーの存在下で、ヒドロホ
ウ酸塩により還元することによって得られる均−系鋼コ
ロイド触媒が、不飽和ニトリルの水利に対し極めて高活
性、高選択性であることを見出した。
Based on these results, the present inventors conducted intensive research and found that a homogeneous steel colloidal catalyst obtained by reducing a copper salt with a hydroborate in the presence of an appropriate protective polymer is unsaturated. It was found that it has extremely high activity and selectivity for nitrile water utilization.

本発明は、かかる知見に基づいて達成されたものであり
、その目的は、アクリルアミドおよび、メタクリルアミ
ドの工業的有用な製造方法を提供することにある。そし
て、この目的は、銅塩を保護ポリマーの存在下、水溶液
中で、ヒドロホウ酸塩により処理して得られる均−系鋼
コロイド水溶液と、アクリロニトリル、または、メタク
リロニトリルを反応させることによって達成される。
The present invention was achieved based on this knowledge, and its purpose is to provide an industrially useful method for producing acrylamide and methacrylamide. This objective is achieved by reacting a homogeneous steel colloid aqueous solution obtained by treating a copper salt with a hydroborate in an aqueous solution in the presence of a protective polymer with acrylonitrile or methacrylonitrile. Ru.

本発明をさらに詳細に説明するに、本発明方法では、触
媒として、銅塩を水溶液中、保護ポリマーの存在下にヒ
ドロホウ酸塩と反応せしめて得られる均−系鋼コロイド
水溶液を使用する。銅塩としては、1価または2価の水
溶性の銅塩、たとえば、硫酸鋼、塩化銅、硝酸銅などを
用いることができる。還元剤としてはアルカリ金属、!
、だは、アルカリ土類金属のヒドロホウ酸塩を通常、水
溶液の状態で使用する。
To explain the invention in more detail, the method of the invention uses as a catalyst an aqueous homogeneous steel colloid solution obtained by reacting a copper salt with a hydroborate salt in an aqueous solution in the presence of a protective polymer. As the copper salt, monovalent or divalent water-soluble copper salts such as steel sulfate, copper chloride, copper nitrate, etc. can be used. Alkali metals as reducing agents!
, alkaline earth metal hydroborates are usually used in aqueous solution.

本発明においては、銅塩とヒドロホウ酸塩との反応を、
保護ポリマーの存在下に行なうことが必要であり、これ
により、均一で安定な銅コロイド水溶液を調製すること
ができる。保護ポリマーとしては、水溶性で保護コロイ
ド作用を有するポリマー、たとえば、ポリ(ビニルピロ
リドン)、ポリ(ビニルアルコール)などが用いられる
In the present invention, the reaction between copper salt and hydroborate is
It is necessary to carry out this process in the presence of a protective polymer, thereby making it possible to prepare a uniform and stable aqueous copper colloid solution. As the protective polymer, a water-soluble polymer having a protective colloid effect, such as poly(vinylpyrrolidone) and poly(vinyl alcohol), is used.

添加する保護ポリマーの量は、銅量に対して通常5〜6
0倍残基当量、好捷しくは10〜40倍残基当量を用い
る。丑だ、銅塩は水11に対して1〜30ミリモル程度
の量を用いるのが適当である。
The amount of protective polymer added is usually 5 to 6 with respect to the amount of copper.
0 times residue equivalents, preferably 10 to 40 times residue equivalents are used. It is appropriate to use the copper salt in an amount of about 1 to 30 mmol per 11 parts of water.

上記ポリマーと銅塩を水に溶解し、しかるのち、ヒドロ
ホウ酸塩の水溶液を加えることによって、即座に均一で
安定な銅コロイド水溶液が得られる。この際加えるヒド
ロホウ酸塩は、還元反応を完定に生起させるため、通常
、銅量に対して2倍モル程度を使用する。さらに多量の
ヒドロホウ酸塩を使用することは、格別の利益をもたら
さないので無意味であり、かつ経済的に不利であるとと
もに、溶液のP■上げるため、好ましくない。また、還
元反応は、通常0〜100℃、好ましくは10〜60℃
で行なわれる。
By dissolving the above polymer and copper salt in water and then adding an aqueous solution of hydroborate, a homogeneous and stable aqueous copper colloid solution is immediately obtained. The hydroborate added at this time is usually used in an amount of about twice the amount of copper in order to cause the reduction reaction to occur completely. The use of even larger amounts of hydroborate is pointless and economically disadvantageous as it does not provide any particular benefits, and is not preferred as it increases the P₁ of the solution. In addition, the reduction reaction is usually 0 to 100°C, preferably 10 to 60°C.
It will be held in

このようにして得られた均−系鋼コロイド水溶液は、不
活性雰囲気下では極めて安定で10日以上室温で放置し
ても変化は見られない。
The homogeneous steel colloid aqueous solution thus obtained is extremely stable under an inert atmosphere, and no change is observed even if it is left at room temperature for 10 days or more.

本発明によれば、かくして得られた触媒の存在下、アク
リロニトリル、または、メタクリロニトリルを水と反応
させる。添加するニトリルは均一液相となる範囲内なら
ば、適当な量を用いることができる。反応の温度および
圧力は、系が液相を保つ広い範囲から選ぶことができる
が、反応速度や反応装置を考慮の上、通常、反応温度は
20〜95℃、反応系の圧力に、減圧〜数気圧で実施さ
れる。なお、反応は、銅が酸化されないように、不活性
雰囲気下で実施する。
According to the invention, acrylonitrile or methacrylonitrile is reacted with water in the presence of the catalyst thus obtained. An appropriate amount of nitrile can be used as long as it forms a uniform liquid phase. The reaction temperature and pressure can be selected from a wide range in which the system remains in a liquid phase, but in consideration of the reaction rate and reaction equipment, the reaction temperature is usually 20 to 95°C, and the pressure of the reaction system is reduced to It is carried out at several atmospheres. Note that the reaction is carried out under an inert atmosphere so that copper is not oxidized.

以上説明したように、本発明によれば、極少量の触媒を
均一に分散させることによって高い活性が得られ、極め
て高い選択率でアクリルアミドを得ることが可能である
。また、従来の方法において、しばしば問題となるエチ
レンシアンヒドリン、アクリル酸、およびオリゴマー類
の生成は、本発明においては検出されなかった。
As explained above, according to the present invention, high activity can be obtained by uniformly dispersing a very small amount of catalyst, and it is possible to obtain acrylamide with extremely high selectivity. Furthermore, the production of ethylene cyanohydrin, acrylic acid, and oligomers, which are often problematic in conventional methods, was not detected in the present invention.

次に本発明を実施例によりさらに詳細に説明するが、本
発明は以下の実施例に限定されるものではない。
Next, the present invention will be explained in more detail with reference to examples, but the present invention is not limited to the following examples.

実施例1 硫酸銅五水和物375m、Pとポリ(ビニルピロリドン
)(重合度3240 ) 0..667 /に水27m
1を加え、完全に溶解させた後、室温でかくはんしなが
ら、テトラヒドロホウ酸ナトリウム11.5 mlを含
む水溶液6mlを加えると、即座に溶液の色が変わり、
黒褐色の均一溶液となった。反応中の系はすべて窒素ガ
ス雰囲気に保った。かくして得られた触媒溶液にアクリ
ロニトリル0.4847’を加え、かきまぜつつ80℃
に2時間保ち反応せしめた。
Example 1 Copper sulfate pentahydrate 375m, P and poly(vinylpyrrolidone) (degree of polymerization 3240) 0. .. 667 / water 27m
After adding 1 and completely dissolving it, 6 ml of an aqueous solution containing 11.5 ml of sodium tetrahydroborate was added while stirring at room temperature, and the color of the solution changed immediately.
The resulting solution became a blackish brown homogeneous solution. All systems during the reaction were kept under nitrogen gas atmosphere. Acrylonitrile 0.4847' was added to the catalyst solution thus obtained, and the mixture was heated to 80°C while stirring.
The mixture was kept for 2 hours to react.

反応終了後、内容物をガスクロマトグラフ法により分析
したところ、アクリロニトリルの反応率215%で、は
ぼ定量的にアクリルアミドが生成しており、副生成物は
検知されなかった。
After the reaction was completed, the contents were analyzed by gas chromatography, and it was found that acrylamide was produced almost quantitatively with a reaction rate of acrylonitrile of 215%, and no by-products were detected.

実施例2 ポリ(ビニルピロリドン)(重合度3240)の量を0
.167 、l’とした以外は実施例1と同様の方法で
、均一溶液として触媒を調製した。これを用いて実施例
1と同一の反応条件下で反応させたところ、アクリロニ
トリル反応率は28.0%でほぼ定量的にアクリルアミ
ドが生成した。副生物の生成は認められなかった。
Example 2 The amount of poly(vinylpyrrolidone) (degree of polymerization 3240) was 0.
.. A catalyst was prepared as a homogeneous solution in the same manner as in Example 1 except that 167 and 1' were used. When this was used to react under the same reaction conditions as in Example 1, the acrylonitrile reaction rate was 28.0%, and acrylamide was produced almost quantitatively. No by-product formation was observed.

比較例1 ポリ(ビニルピロリドン)を使用しない以外は、実施例
1と同様にして、硫酸銅五水和物675m!トチトラヒ
ドロホウ酸ナトリウム1 i、 3 m、Pより、黒色
沈殿として触媒を調製した。これを用いて実施例1と同
一の反応条件で反応をさせたところ、アクリルアミドの
生成率は4.4%でありエチレンシアンヒドリンの生成
が01%認められた。
Comparative Example 1 Copper sulfate pentahydrate 675m! was prepared in the same manner as in Example 1 except that poly(vinylpyrrolidone) was not used. A catalyst was prepared from sodium totitrahydroborate 1 i, 3 m, P as a black precipitate. When this was used to carry out a reaction under the same reaction conditions as in Example 1, the production rate of acrylamide was 4.4%, and the production of ethylene cyanohydrin was observed at 0.1%.

特許出願人 平井英史 347−Patent applicant Hidefumi Hirai 347-

Claims (1)

【特許請求の範囲】[Claims] 選ばれた銅塩を保護コロイド作用を有する高分子の存在
下、アルカリ金属、または、アルカリ土類金属のヒドロ
ホウ酸塩で処理して得られる均−系鋼コロイドを触媒と
して用いることを特徴とするz1アクリロニトリル、ま
たは、メタクリロニトリルの水利によりアクリルアミド
、または、メタクリルアミドを製造する方法
A homogeneous steel colloid obtained by treating a selected copper salt with an alkali metal or alkaline earth metal hydroborate in the presence of a polymer having a protective colloid action is used as a catalyst. z1 Method for producing acrylamide or methacrylamide by water utilization of acrylonitrile or methacrylonitrile
JP57141875A 1982-08-16 1982-08-16 Preparation of unsaturated amide Pending JPS5931742A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57141875A JPS5931742A (en) 1982-08-16 1982-08-16 Preparation of unsaturated amide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57141875A JPS5931742A (en) 1982-08-16 1982-08-16 Preparation of unsaturated amide

Publications (1)

Publication Number Publication Date
JPS5931742A true JPS5931742A (en) 1984-02-20

Family

ID=15302189

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57141875A Pending JPS5931742A (en) 1982-08-16 1982-08-16 Preparation of unsaturated amide

Country Status (1)

Country Link
JP (1) JPS5931742A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0695579A1 (en) 1994-08-02 1996-02-07 MITSUI TOATSU CHEMICALS, Inc. Copper catalyst for the hydration of nitrile and preparation thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0695579A1 (en) 1994-08-02 1996-02-07 MITSUI TOATSU CHEMICALS, Inc. Copper catalyst for the hydration of nitrile and preparation thereof

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