JPH06173056A - Production of alkylurea compound by electroysis - Google Patents

Production of alkylurea compound by electroysis

Info

Publication number
JPH06173056A
JPH06173056A JP4329378A JP32937892A JPH06173056A JP H06173056 A JPH06173056 A JP H06173056A JP 4329378 A JP4329378 A JP 4329378A JP 32937892 A JP32937892 A JP 32937892A JP H06173056 A JPH06173056 A JP H06173056A
Authority
JP
Japan
Prior art keywords
alkylamine
carbon monoxide
alkylurea
electrolytic
production
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
JP4329378A
Other languages
Japanese (ja)
Inventor
Atsushi Okamoto
淳 岡本
Masanori Takemoto
眞規 竹本
Tetsuo Aoyama
哲男 青山
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 Gas Chemical Co Inc
Original Assignee
Mitsubishi Gas Chemical Co 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 Mitsubishi Gas Chemical Co Inc filed Critical Mitsubishi Gas Chemical Co Inc
Priority to JP4329378A priority Critical patent/JPH06173056A/en
Publication of JPH06173056A publication Critical patent/JPH06173056A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To produce an alkylurea compd. under mild conditions by electrolyzing carbon monoxide and an alkylamine with an anode contg. a Pt group element. CONSTITUTION:Carbon monoxide and an alkylamine such as methylamine, dimethylamine or ethylamine are electrolyzed with an anode contg. a Pt group element such as Pd, Pt or Ru. At this time, methanol acetonitrile or the like is used as a solvent, sodium iodide or the like is used as a supporting electrolyte and conditions in electrolysis are regulated to about 0-100 deg.C temp., about 1-20atm pressure and about 1-20A/dm<2> current density. The objective alkylurea compd. is easily produced under mild conditions.

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、医薬品、農薬、染料等
の合成原料として有用なアルキル尿素化合物を、一酸化
炭素とアルキルアミンから電解反応により製造する方法
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing an alkylurea compound useful as a synthetic raw material for pharmaceuticals, agricultural chemicals, dyes and the like from carbon monoxide and an alkylamine by an electrolytic reaction.

【0002】[0002]

【従来の技術】従来、アルキル尿素化合物の製造方法と
しては、1)アルキルアミンと二酸化炭素を反応させる
方法(特公昭62−9107号)、2)アルキルアミン
と尿素を反応させる方法(特公平2−7945号)、
3)アルキルアミンと一酸化炭素及び酸素を反応させる
方法(特公平2−57064号、J. Am. Chem.
Soc.,93, 6344(1971)等が知られてい
る。しかしながら、1)、2)の方法は高温高圧の反応
条件を必要とする。3)の方法は一酸化炭素と酸素の混
合ガスを加熱して使用するために爆発等の危険性があ
り、さらに触媒として毒性の強いセレン等を使用する等
の問題点がある。
2. Description of the Related Art Conventionally, as a method for producing an alkylurea compound, 1) a method of reacting an alkylamine with carbon dioxide (Japanese Patent Publication No. 62-9107), and 2) a method of reacting an alkylamine with urea (Japanese Patent Publication No. 2). -7945),
3) Method of reacting alkylamine with carbon monoxide and oxygen (Japanese Patent Publication No. 2-57064, J. Am. Chem.
Soc., 93, 6344 (1971) and the like are known. However, the methods 1) and 2) require high temperature and high pressure reaction conditions. The method 3) has a risk of explosion and the like because a mixed gas of carbon monoxide and oxygen is heated and used, and further, there is a problem that selenium or the like having strong toxicity is used as a catalyst.

【0003】[0003]

【発明が解決しようとする課題】本発明は、従来技術に
おける上記の如き種々の課題点を解決し、温和でかつ簡
便なアルキル尿素の製造法を開発するものであり、一酸
化炭素とアルキルアミンから温和な条件下において、好
成績を以てアルキル尿素化合物を電解製造する方法を提
供する。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned various problems in the prior art and develops a mild and convenient method for producing an alkylurea, which comprises carbon monoxide and an alkylamine. To provide a method for electrolytically producing an alkylurea compound with good results under mild conditions.

【0004】[0004]

【課題を解決するための手段】本発明者らは、上記課題
を解決するために鋭意研究を重ねた結果、白金族元素を
含有する陽極を用いて、一酸化炭素とアルキルアミンを
電解することにより、温和な条件下でアルキル尿素化合
物が生成することを見い出し、本発明に到達し完成させ
た。本発明におけるアルキル尿素化合物の生成反応は、
下式によって表すことができる。
Means for Solving the Problems As a result of intensive studies to solve the above problems, the present inventors have found that an anode containing a platinum group element is used to electrolyze carbon monoxide and an alkylamine. As a result, they found that an alkylurea compound was produced under mild conditions, and reached and completed the present invention. The production reaction of the alkylurea compound in the present invention is
It can be represented by the following formula.

【0005】[0005]

【化1】2HNRR’+ CO → RR’NC(O)
NRR’+ H2 式中、R、R’は水素または炭素数1から8のアルキル
基であって、更に互いに同種または異種のものであって
もよい。
[Chemical formula 1] 2HNRR '+ CO → RR'NC (O)
NRR ′ + H 2 In the formula, R and R ′ are hydrogen or an alkyl group having 1 to 8 carbon atoms, and may be the same or different from each other.

【0006】本発明で用いられるアルキルアミンは、炭
素数1〜8からなる一級もしくは二級の脂肪族アミンで
あって、具体的にはメチルアミン、ジメチルアミン、エ
チルアミン、ジエチルアミン、プロピルアミン、ジプロ
ピルアミン、ブチルアミン、ジブチルアミン等が挙げら
れる。
The alkylamine used in the present invention is a primary or secondary aliphatic amine having 1 to 8 carbon atoms, specifically, methylamine, dimethylamine, ethylamine, diethylamine, propylamine, dipropyl. Examples thereof include amine, butylamine, dibutylamine and the like.

【0007】本発明の方法において、陽極に使用される
白金族元素は、パラジウム、プラチナ、ルテニウム、ロ
ジウム、イリジウム、オスミウムであり、これらの金属
または化合物を用いることができる。 化合物の例とし
ては酸化物、ハロゲン化物、硝酸塩、錯体化合物などが
挙げられる。 また、これらの元素のうち一つ又は複数
を組合わせて使用することが可能であり、これらの白金
族元素を含有する電極であれば、形状等には特に制限は
なく、白金族元素の金属膜、又は通常の電解製造法に用
いられる電極上に白金族元素を蒸着、又はメッキ、又は
圧着したもの、もしくはそれらの化合物を担持したもの
等を用いることができる。
In the method of the present invention, the platinum group element used for the anode is palladium, platinum, ruthenium, rhodium, iridium or osmium, and these metals or compounds can be used. Examples of the compound include oxides, halides, nitrates, complex compounds and the like. Further, it is possible to use one or more of these elements in combination, and there is no particular limitation on the shape or the like as long as it is an electrode containing these platinum group elements. It is possible to use, for example, a film, or an electrode used in a usual electrolytic production method, on which a platinum group element is vapor-deposited, plated, or pressure-bonded, or those compounds are supported.

【0008】本発明で用いられる溶媒は、通常の電解製
造法で用いられるような溶媒であれば特に制限はない
が、溶媒の関与した副反応を避けるために原料のアルキ
ルアミンよりも酸化ポテンシャルが低いものを用いるこ
とが望ましい。 例としてはアセトニトリル、ジメチル
ホルムアミド、メタノール等が挙げられる。 また、ア
ルキルアミンそのものを電解溶媒として用いることも可
能である。
The solvent used in the present invention is not particularly limited as long as it is a solvent used in a usual electrolytic production method, but has an oxidation potential higher than that of the starting alkylamine in order to avoid side reactions involving the solvent. It is desirable to use a low one. Examples include acetonitrile, dimethylformamide, methanol and the like. It is also possible to use the alkylamine itself as the electrolytic solvent.

【0009】本発明に用いられる支持電解質は、溶媒及
び原料のアミンに溶解するものであれば特に制限はな
く、カチオン成分として周期律表第1A族元素のイオ
ン、四級アルキルアンモニウムイオン等、アニオン成分
として塩素イオン、臭素イオン、ヨウ素イオン等の組合
わせからなる支持電解質を用いることができる。アニオ
ン成分の中では、特にヨウ素イオンがアルキル尿素化合
物への選択性が高く好ましい。 また本発明における支
持電解質は、原料のアミンに対して0. 1〜20重量%
であることが好ましい。
The supporting electrolyte used in the present invention is not particularly limited as long as it can be dissolved in a solvent and an amine as a raw material, and as a cation component, an anion such as an ion of a Group 1A element of the periodic table, a quaternary alkylammonium ion or the like, an anion. A supporting electrolyte composed of a combination of chlorine ion, bromine ion, iodine ion and the like can be used as a component. Among the anion components, iodide ion is particularly preferable because it has high selectivity for the alkylurea compound. The supporting electrolyte in the present invention is 0.1 to 20% by weight based on the raw material amine.
Is preferred.

【0010】本発明に使用される電解槽は、隔膜型、無
隔膜型いずれのタイプのものも使用できるが、経済性等
の点から無隔膜型電解槽を用いることが好ましい。隔膜
型電解槽を用いる場合の隔膜の材質については、通常の
電解製造法に用いられるものであれば特に制限はない。
電極対の形状や配置及び通電方法については通常の電
解製造法に採用される形式を用いることができる。特に
陽極と陰極の間隔は、電流効率及び電圧効率を良くする
ために極力小さいことが望ましく、実用的にはキャピラ
リーギャップセル等の使用が好ましい。電極対への通電
方法は単極式、複極式のいずれの方法でも良く、経済的
に有効な方法を選択することができる。
The electrolytic cell used in the present invention may be either a diaphragm type or a diaphragmless type, but it is preferable to use the diaphragmless electrolytic cell from the viewpoint of economy. The material of the diaphragm in the case of using the diaphragm type electrolytic cell is not particularly limited as long as it is used in a usual electrolytic production method.
With respect to the shape and arrangement of the electrode pair and the energization method, the type adopted in a usual electrolytic manufacturing method can be used. In particular, the distance between the anode and the cathode is preferably as small as possible in order to improve the current efficiency and the voltage efficiency, and it is practically preferable to use a capillary gap cell or the like. The method of energizing the electrode pair may be either a monopolar method or a bipolar method, and an economically effective method can be selected.

【0011】本発明に用いられる一酸化炭素は、純度が
高い方が望ましいが、アルキルアミンの酸化等の副反応
が進行するのを防ぐために、酸化性ガスを極力含まない
ことが望ましい。 また、電解槽内における一酸化炭素
とアルキルアミンのモル比については、両者が共存して
いれば特に制限はないが、一酸化炭素が多い条件が好ま
しい。
The carbon monoxide used in the present invention preferably has a high purity, but it is desirable that the carbon monoxide does not contain oxidizing gas as much as possible in order to prevent the progress of side reactions such as oxidation of alkylamine. Further, the molar ratio of carbon monoxide and alkylamine in the electrolytic cell is not particularly limited as long as both coexist, but a condition with a large amount of carbon monoxide is preferable.

【0012】本発明における電解温度、電解圧力、電流
密度の条件は、特に制限はないが、0〜100℃、1〜
20気圧、1〜20A/dm2 の範囲であれば良い。一
酸化炭素、及び低級アルキルアミンをガス成分として電
解槽へ供給する場合には、常圧であっても反応は進行す
るが、電解溶媒への充分な溶解量を得るために若干の加
圧条件下が好ましい。
The conditions of electrolysis temperature, electrolysis pressure and current density in the present invention are not particularly limited, but are 0 to 100 ° C., 1 to
The pressure may be in the range of 20 atm and 1 to 20 A / dm 2 . When carbon monoxide and lower alkylamine are supplied to the electrolytic cell as gas components, the reaction proceeds even at normal pressure, but some pressurization conditions are required to obtain a sufficient amount of dissolution in the electrolytic solvent. Lower is preferred.

【0013】[0013]

【発明の効果】白金族元素を含有する陽極を用いて電解
反応を行うことにより、温和な条件下で一酸化炭素とア
ルキルアミンからアルキル尿素化合物を製造することが
可能になった。
By carrying out an electrolytic reaction using an anode containing a platinum group element, it has become possible to produce an alkylurea compound from carbon monoxide and an alkylamine under mild conditions.

【0014】[0014]

【実施例】以下に実施例に基づき本発明を具体的に説明
するが、本発明はこれらの実施例に制限されるものでは
ない。実施例1 250mlのセパラブルフラスコにメタノール184
g、ヨウ化ナトリウム3. 8gを採り混合した。 幾何
表面積が約17cm2 の長方形パラジウム金属膜電極
(0. 2mm厚)と炭素電極の2枚を極間距離4mmで
固定し、各々を陽極、陰極として結線し、上記の電解液
中に浸した。 モノメチルアミンを循環させ電解液中に
溶解させた。 溶解量は3. 8gであった。 そこに一
酸化炭素1. 8Lを常圧下でバブリングさせながら循環
させ、電流密度5. 8A/dm2にて定電流制御で直流
電流を通電した。 電解反応中は電解電圧はほぼ7Vの
値であった。 液の撹拌はマグネチックスターラーで行
い、水浴によって電解反応中の電解液の温度を約15〜
25℃に保った。49. 7mF通電後、電解液中に1.
6gの1, 3- ジメチル尿素と0. 05gのN- メチル
カルバミン酸メチルの生成が、また循環ガス中に0. 0
4gの水素の生成が認められた。 電流効率は73%で
あった。
EXAMPLES The present invention will be specifically described below based on examples, but the present invention is not limited to these examples. Example 1 Methanol 184 was added to a 250 ml separable flask.
g and 3.8 g of sodium iodide were taken and mixed. Two rectangular palladium metal membrane electrodes (0.2 mm thick) having a geometric surface area of about 17 cm 2 and carbon electrodes were fixed with a distance between electrodes of 4 mm, and each was connected as an anode and a cathode and immersed in the above electrolyte solution. . Monomethylamine was circulated and dissolved in the electrolytic solution. The dissolved amount was 3.8 g. There, 1.8 L of carbon monoxide was circulated while bubbling under normal pressure, and a direct current was passed under constant current control at a current density of 5.8 A / dm 2 . The electrolysis voltage was about 7 V during the electrolysis reaction. The liquid is stirred with a magnetic stirrer, and the temperature of the electrolytic solution during the electrolytic reaction is about 15
It was kept at 25 ° C. 49.7mF After energizing, 1.
The formation of 6 g of 1,3-dimethylurea and 0.05 g of methyl N-methylcarbamate also leads to 0.0
The production of 4 g of hydrogen was observed. The current efficiency was 73%.

【0015】実施例2 実施例1と同じ電解装置、手法を用いてジメチルアミン
5.2gを含むメタノール180g,ヨウ化ナトリウム
3.8gからなる電解液に一酸化炭素1.8Lを常圧下
でバブリングさせながら循環させ、電流密度5.8A/
dm2 で通電した。 電解反応中は電解電圧は7〜8V
の値であった。60. 4mF通電後、電解液中に1. 9
gの1, 1, 3, 3- テトラメチル尿素と0. 35gの
N, N- ジメチルカルバミン酸メチルの生成が、また循
環ガス中に0. 05gの水素の生成が認められた。 電
流効率は54%であった。
Example 2 Using the same electrolytic apparatus and method as in Example 1, 1.8 L of carbon monoxide was bubbled into an electrolytic solution containing 180 g of methanol containing 3.8 g of dimethylamine and 3.8 g of sodium iodide under normal pressure. While circulating, current density is 5.8A /
Energized at dm 2 . The electrolysis voltage is 7 to 8V during the electrolysis reaction.
Was the value of. After energizing at 60.4 mF, it is 1.9 in the electrolyte.
The production of g of 1,1,3,3-tetramethylurea and 0.35 g of methyl N, N-dimethylcarbamate and the production of 0.05 g of hydrogen in the circulating gas were observed. The current efficiency was 54%.

【0016】実施例3 陽極にチタン板上に白金メッキしたもの(幾何表面積約
17cm2 ) を用い、実施例1と同じ電解装置、手法を
用いてメチルアミン3. 5gを含むメタノール181
g、ヨウ化ナトリウム3. 8gからなる電解液に一酸化
炭素1. 8Lをバブリングさせながら循環させ、電流密
度5. 8A/dm2 で通電した。19. 4mF通電後、
電解液中に0. 55gの1, 3- ジメチル尿素の生成が
認められた。 電流効率は64%であった。
Example 3 Using a platinum plate on a titanium plate (geometric surface area of about 17 cm 2 ) as an anode, and using the same electrolytic apparatus and method as in Example 1, methanol 181 containing 3.5 g of methylamine was used.
g, and 1.8 g of carbon monoxide were circulated while bubbling through an electrolytic solution containing 3.8 g of sodium iodide, and electricity was supplied at a current density of 5.8 A / dm 2 . After energizing 19.4 mF,
Formation of 0.55 g of 1,3-dimethylurea was observed in the electrolytic solution. The current efficiency was 64%.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】白金族元素を含有する陽極を用いて、一酸
化炭素とアルキルアミンから、電解反応によりアルキル
尿素化合物を製造する方法。
1. A method for producing an alkylurea compound from carbon monoxide and an alkylamine by an electrolytic reaction using an anode containing a platinum group element.
JP4329378A 1992-12-09 1992-12-09 Production of alkylurea compound by electroysis Pending JPH06173056A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4329378A JPH06173056A (en) 1992-12-09 1992-12-09 Production of alkylurea compound by electroysis

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4329378A JPH06173056A (en) 1992-12-09 1992-12-09 Production of alkylurea compound by electroysis

Publications (1)

Publication Number Publication Date
JPH06173056A true JPH06173056A (en) 1994-06-21

Family

ID=18220776

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4329378A Pending JPH06173056A (en) 1992-12-09 1992-12-09 Production of alkylurea compound by electroysis

Country Status (1)

Country Link
JP (1) JPH06173056A (en)

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