JPH04308582A - Production of 4-amino-1,2,4-triazole - Google Patents

Production of 4-amino-1,2,4-triazole

Info

Publication number
JPH04308582A
JPH04308582A JP15082391A JP15082391A JPH04308582A JP H04308582 A JPH04308582 A JP H04308582A JP 15082391 A JP15082391 A JP 15082391A JP 15082391 A JP15082391 A JP 15082391A JP H04308582 A JPH04308582 A JP H04308582A
Authority
JP
Japan
Prior art keywords
reaction
hydrazine
formic acid
organic solvent
triazole
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
JP15082391A
Other languages
Japanese (ja)
Inventor
Rikuo Nasu
那須 陸男
Taku Shimura
志村 卓
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.)
Ishihara Sangyo Kaisha Ltd
Original Assignee
Ishihara Sangyo Kaisha 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 Ishihara Sangyo Kaisha Ltd filed Critical Ishihara Sangyo Kaisha Ltd
Priority to JP15082391A priority Critical patent/JPH04308582A/en
Publication of JPH04308582A publication Critical patent/JPH04308582A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To produce the subject compound useful as a raw material for nitration-reducing agents, medicines, agricultural chemicals, UV ray absorbents, etc., in high yield and high purity by reacting formic acid. etc., with hydrazine in an organic solvent under heating. CONSTITUTION:Formic acid, an ester thereof (e.g. methyl ester, ethyl ester or an amide (e.g. formamide, dimethyl formamide) with hydrazine in an organic solvent (preferably a solvent having a boiling point of >=130 deg.C, e.g. xylene, mesitylene, chlorobenzene preferably at 130-170 deg.C for 2-20hr to provide the objective compound.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は硝酸化成抑制剤として或
いは医薬、農薬、紫外線吸収剤などの原料として有用な
4−アミノ−1,2,4−トリアゾールの製造方法に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing 4-amino-1,2,4-triazole, which is useful as a nitrification inhibitor or as a raw material for medicines, agricultural chemicals, ultraviolet absorbers, and the like.

【0002】0002

【従来の技術】従来から4−アミノ−1,2,4−トリ
アゾールの製造については種々の方法が知られている。 例えば特公昭46−35056号公報には蟻酸とヒドラ
ジンとを燐酸の存在下に190℃以下で反応させること
により4−アミノ−1,2,4−トリアゾールを製造す
る方法が記載されている。
BACKGROUND OF THE INVENTION Various methods have been known for producing 4-amino-1,2,4-triazole. For example, Japanese Patent Publication No. 46-35056 describes a method for producing 4-amino-1,2,4-triazole by reacting formic acid and hydrazine in the presence of phosphoric acid at 190°C or lower.

【0003】0003

【発明が解決しようとする問題点】しかしながら前述の
製造方法においては少量の燐酸が生成物に混入ししかも
この燐酸は分離、除去し難いために目的物の品質面で問
題があり、また副生する水を反応系外に留去する際しば
しば突沸が生じるために操業面でも問題がある。一方、
燐酸を存在させずに前述の反応を行なった場合、目的物
の収率が低下するために望ましくない。
[Problems to be Solved by the Invention] However, in the above-mentioned manufacturing method, a small amount of phosphoric acid is mixed into the product, and this phosphoric acid is difficult to separate and remove, causing problems in terms of the quality of the target product, and also by-products. Bumping often occurs when water is distilled out of the reaction system, which poses operational problems. on the other hand,
It is undesirable to carry out the above reaction without the presence of phosphoric acid because the yield of the target product decreases.

【0004】0004

【問題点を解決するための手段】本発明者達は前述の製
造方法において燐酸を使用せず有機溶媒の存在下に反応
させたところ、勿論、燐酸のような狭雑物を含まない品
質の高い生成物が高い収率で得られ、また副生する水も
簡単に除去でき、蒸留操作においても突沸は発生せず円
滑に水を留去できることを見出した。
[Means for Solving the Problems] The present inventors conducted the reaction in the presence of an organic solvent without using phosphoric acid in the above-mentioned production method. It has been found that a high product can be obtained in a high yield, water as a by-product can be easily removed, and water can be smoothly distilled off without bumping during the distillation operation.

【0005】本発明は蟻酸、そのエステル類又はアミド
類とヒドラジンとを加熱下に反応させて4−アミノ−1
,2,4−トリアゾールを製造する方法において、有機
溶媒の存在下に反応を行なうことを特徴とする4−アミ
ノ−1,2,4−トリアゾールの製造方法である。
The present invention involves reacting formic acid, its esters or amides with hydrazine under heating to produce 4-amino-1
, 2,4-triazole, the method is characterized in that the reaction is carried out in the presence of an organic solvent.

【0006】本発明においては蟻酸、そのエステル類又
はアミド類とヒドラジンとを有機溶媒の存在下に加熱す
ることにより反応させるが、各原料物質及び有機溶媒の
添加順序は問わず、例えば両原料物質及び有機溶媒を一
度に混合したり或はヒドラジン及び有機溶媒を一旦混合
した混合物と蟻酸、そのエステル類又はアミド類とを混
合したりする。
[0006] In the present invention, formic acid, its esters or amides are reacted with hydrazine by heating in the presence of an organic solvent, but the order in which each raw material and organic solvent are added does not matter. and an organic solvent at once, or a mixture of hydrazine and an organic solvent is mixed with formic acid, its esters or amides.

【0007】本発明で使用する各原料物質については次
に例示されるが、反応目的、反応条件などに応じて適宜
選択されうる。蟻酸以外に蟻酸のエステル類及びアミド
類としては蟻酸のメチルエステル、エチルエステルなど
の蟻酸のアルキルエステル類:ホルムアミド、ジチルホ
ルムアミドなどの蟻酸のアミド類が挙げられるが、蟻酸
及びそのアミド類が望ましく、なかでも蟻酸及びジメチ
ルホルムアミドがより望ましい。またヒドラジンとして
は無水ヒドラジンは空気中で強く発煙して取扱いに難点
があるため抱水ヒドラジンが望ましい。
[0007] Each raw material used in the present invention is exemplified below, and can be appropriately selected depending on the purpose of the reaction, reaction conditions, etc. Examples of esters and amides of formic acid other than formic acid include alkyl esters of formic acid such as methyl ester and ethyl ester of formic acid; amides of formic acid such as formamide and dithylformamide; preferably, formic acid and its amides; Among these, formic acid and dimethylformamide are more desirable. Further, as the hydrazine, hydrated hydrazine is preferable because anhydrous hydrazine emits strong smoke in the air and is difficult to handle.

【0008】更に本発明で使用する有機溶媒については
反応に不活性なものであればいずれのものでもよいが、
水及び目的物4−アミノ−1,2,4−トリアゾールに
不溶乃至難溶で沸点が130℃以上のものが望ましく、
例えばキシレン、メシチレン、クロロベンゼン、o,m
,p−ジクロロベンゼン、1,2,4−、1,3,5−
トリクロロベンゼン、o,m,p−クロロトルエンなど
の芳香族炭化水素、デカン、ウンデカンなどの脂肪族飽
和炭化水素などが挙げられるが、勿論、それらの混合物
であってもよい。
Furthermore, the organic solvent used in the present invention may be any organic solvent as long as it is inert to the reaction.
It is preferable that it is insoluble or poorly soluble in water and the target substance 4-amino-1,2,4-triazole and has a boiling point of 130°C or higher.
For example, xylene, mesitylene, chlorobenzene, o, m
, p-dichlorobenzene, 1,2,4-, 1,3,5-
Examples include aromatic hydrocarbons such as trichlorobenzene, o, m, p-chlorotoluene, and aliphatic saturated hydrocarbons such as decane and undecane, but of course, mixtures thereof may be used.

【0009】本発明においては原料物質及び有機溶媒の
使用量はそれらの種類、反応条件などの相違により異な
り一概に規定できないが、蟻酸、そのエステル類又はア
ミド類1モルに対しヒドラジンは普通0.8〜1.5モ
ル望ましくは1モル前後であり、また有機溶媒は普通5
〜500重量部好ましくは30〜100重量部である。
In the present invention, the amounts of raw materials and organic solvents to be used vary depending on their types, reaction conditions, etc., and cannot be unconditionally defined, but the amount of hydrazine used is usually 0.0% per mole of formic acid, its esters, or amides. The amount is preferably 8 to 1.5 mol, preferably around 1 mol, and the organic solvent is usually 5 mol.
-500 parts by weight, preferably 30-100 parts by weight.

【0010】本発明の反応の反応条件は同様に一概に規
定できないが、反応温度は130〜190℃望ましくは
130〜170℃、反応時間は2〜20時間である。反
応は通常、反応混合物のヒドラジンが消失する迄、反応
中に副生した水を還流することにより行なわれるが、大
量の溶媒が存在するため突沸は防止できると共に局部加
熱による目的物の分解、副反応の発生も防止することが
できる。
[0010] Although the reaction conditions for the reaction of the present invention cannot be defined unconditionally, the reaction temperature is preferably 130 to 190°C, preferably 130 to 170°C, and the reaction time is 2 to 20 hours. The reaction is usually carried out by refluxing the water produced as a by-product during the reaction until the hydrazine in the reaction mixture disappears, but the presence of a large amount of solvent prevents bumping and prevents decomposition of the target product and by-products due to local heating. The occurrence of reactions can also be prevented.

【0011】また本発明では一般に反応生成物に目的物
の4−アミノ−1,2,4−トリアゾールが溶媒及び水
に殆んど溶解せずに存在するために分液により目的物を
容易に分離することができるが、更に必要ならば溶媒を
留去することにより目的物を回収してもよい。かくして
目的物の4−アミノ−1,2,4−トリアゾールは例え
ば収率91%以上、純度91%以上で得ることができる
。
In addition, in the present invention, the target product, 4-amino-1,2,4-triazole, is generally present in the reaction product with almost no solubility in the solvent and water, so the target product can be easily obtained by liquid separation. If necessary, the target product may be recovered by distilling off the solvent. In this way, the target product, 4-amino-1,2,4-triazole, can be obtained, for example, in a yield of 91% or more and a purity of 91% or more.

【0012】次に本発明に係る実施例を記載するが、本
発明はこれら記載に限定されるものではない。
[0012] Next, examples according to the present invention will be described, but the present invention is not limited to these descriptions.

【0013】実施例1 攪拌装置、温度計、冷却管及び滴下ロートを備えた20
00ml容四つ口フラスコに80%ヒドラジン・一水和
物  514g(8.23mol)及びキシレン600
gを室温で仕込んだ。87%ギ酸  435g(8.2
3mol)を滴下ロートで30分間かけて攪拌しながら
滴下したところ、発熱があり、90℃まで上昇した。そ
の後加熱し、105℃で3時間攪拌を継続した。この間
、生成水は冷却管で系内に戻した。そして、冷却管を、
上部に冷却管を備えた水分定量受器(生成水のみを系外
に除去し、溶媒は系内に戻す)に交換し、138℃まで
加熱したのち、その温度でヒドラジンの濃度が1%以下
になるまで反応を継続した。138℃での反応時間は1
5時間であった。
Example 1 20 units equipped with a stirrer, a thermometer, a cooling tube and a dropping funnel
514 g (8.23 mol) of 80% hydrazine monohydrate and 600 g of xylene in a 00 ml four-necked flask.
g was prepared at room temperature. 87% formic acid 435g (8.2
When 3 mol) was added dropwise with stirring over 30 minutes using a dropping funnel, heat generation occurred and the temperature rose to 90°C. Thereafter, the mixture was heated and stirring was continued at 105° C. for 3 hours. During this time, the produced water was returned to the system through a cooling pipe. Then, the cooling pipe
Replace it with a moisture metering receiver equipped with a cooling pipe at the top (remove only the produced water from the system and return the solvent to the system) and heat it to 138°C. At that temperature, the concentration of hydrazine is 1% or less. The reaction was continued until The reaction time at 138℃ is 1
It was 5 hours.

【0014】反応終了後、100℃まで冷却し、分液に
より下層の目的物を分別した。若干キシレンが含まれて
いるため、キシレンを減圧下に除去した。目的物が33
6g(粗収率97.2%)得られ、純度は93.1%で
あった。
After the reaction was completed, the mixture was cooled to 100° C. and the target product in the lower layer was separated by liquid separation. Since it contained some xylene, xylene was removed under reduced pressure. The target is 33
6 g (crude yield 97.2%) was obtained, and the purity was 93.1%.

【0015】実施例2 攪拌装置、温度計、冷却管及び滴下ロートを備えた20
0ml容四つ口フラスコに80%ヒドラジン・一水和物
  62.5g(1.0mol)及びISOPAR−G
  75gを室温で仕込んだ。87%ギ酸  52.9
g(1.0mol)を滴下ロートで10分間かけて撹拌
しながら滴下したところ、発熱があり、80℃まで上昇
した。その後加熱し、105℃で3時間撹拌を継続した
。 この間、生成水は冷却管で系内に戻した。そして、冷却
管を、実施例1と同様の上部に冷却管を備えた水分定量
受器に交換し、165℃まで加熱したのち、その温度で
ヒドラジンの濃度が1%以下になるまで反応を継続した
。165℃での反応時間は6時間であった。
Example 2 20 units equipped with a stirrer, thermometer, cooling tube and dropping funnel
62.5 g (1.0 mol) of 80% hydrazine monohydrate and ISOPAR-G in a 0 ml four-necked flask.
75g was charged at room temperature. 87% formic acid 52.9
When the mixture was added dropwise with stirring over 10 minutes using a dropping funnel, heat generation occurred and the temperature rose to 80°C. Thereafter, the mixture was heated and stirring was continued at 105° C. for 3 hours. During this time, the produced water was returned to the system through a cooling pipe. Then, the cooling tube was replaced with a water quantitative receiver equipped with a cooling tube at the top similar to that in Example 1, and after heating to 165°C, the reaction was continued at that temperature until the concentration of hydrazine became 1% or less. did. The reaction time at 165°C was 6 hours.

【0016】反応終了後、100℃まで冷却し、分液に
より下層の目的物を分別した。若干ISOPAR−Gが
含まれているため、ISOPAR−Gを減圧下に除去し
た。目的物が38.5g(粗収率91.7%)得られ、
純度は95.4%であった。
After the reaction was completed, the mixture was cooled to 100° C. and the target product in the lower layer was separated by liquid separation. Since some ISOPAR-G was contained, ISOPAR-G was removed under reduced pressure. 38.5g (crude yield 91.7%) of the target product was obtained,
Purity was 95.4%.

【0017】ISOPAR−G  平均分子量149の
脂肪族飽和炭化水素  炭素数10〜11比重0.75
0、引火点41℃、アニリン点41℃、蒸留範囲(初留
点158℃、5%−160℃、10%−161℃、50
%−164℃、90%−170℃及び95%−173℃
)エクソン化学株式会社の商品
ISOPAR-G Aliphatic saturated hydrocarbon with average molecular weight 149, carbon number 10-11, specific gravity 0.75
0, flash point 41℃, aniline point 41℃, distillation range (initial boiling point 158℃, 5%-160℃, 10%-161℃, 50
%-164℃, 90%-170℃ and 95%-173℃
) Products of Exxon Chemical Co., Ltd.

【0018】実施例3 攪拌装置、温度計、冷却管及び滴下ロートを備えた10
00ml容四つ口フラスコに80%ヒドラジン・一水和
物  93.8g(1.5mol)、ジメチルホルムア
ミド(DMF)131.6g(1.8mol)及びキシ
レン130gを室温で仕込んだが、発熱は認められなか
った。攪拌を開始し、加熱して100℃で3時間還流し
ながら反応を行った。そして、冷却管を実施例1と同様
の上部に冷却管を備えた水分定量受器に交換し、138
℃まで加熱したのち、その温度でヒドラジンの濃度が1
%以下になるまで反応を継続した。138℃での反応時
間は18時間であった。
Example 3 10 equipped with a stirrer, thermometer, cooling tube and dropping funnel
93.8 g (1.5 mol) of 80% hydrazine monohydrate, 131.6 g (1.8 mol) of dimethylformamide (DMF), and 130 g of xylene were charged into a 00 ml four-necked flask at room temperature, but no heat generation was observed. There wasn't. Stirring was started, and the reaction was carried out while heating and refluxing at 100° C. for 3 hours. Then, the cooling pipe was replaced with a moisture metering receiver equipped with a cooling pipe on the upper part as in Example 1.
After heating to ℃, the concentration of hydrazine becomes 1 at that temperature.
The reaction was continued until the concentration decreased to below %. The reaction time at 138°C was 18 hours.

【0019】反応終了後、100℃まで冷却し、分液に
より下層の目的物を分別した。若干キシレンが含まれて
いるため、キシレンを減圧下に除去した。目的物が57
.7g(粗収率91.6%)得られ、純度は91.0%
であった。
After the reaction was completed, the mixture was cooled to 100° C. and the target product in the lower layer was separated by liquid separation. Since it contained some xylene, xylene was removed under reduced pressure. The target is 57
.. 7g (crude yield 91.6%) obtained, purity 91.0%
Met.

【0020】実施例4 攪拌装置、温度計、冷却管及び滴下ロートを備えた10
00ml容四つ口フラスコに80%ヒドラジン・一水和
物  93.8g(1.5mol)、ジメチルホルムア
ミド(DMF)110g(1.5mol)及び前記実施
例1と同様のISOPAR−G  113gを室温で仕
込んだが、発熱は認められなかった。攪拌を開始し、加
熱して105℃で3時間加熱還流しながら反応を行った
。そして、冷却管を実施例1と同様の上部に冷却管を備
えた水分定量受器に交換し、160℃まで加熱したのち
、その温度でヒドラジンの濃度が1%以下になるまで反
応を継続した。160℃での反応時間は8時間であった
。
Example 4 10 equipped with a stirrer, thermometer, cooling tube and dropping funnel
93.8 g (1.5 mol) of 80% hydrazine monohydrate, 110 g (1.5 mol) of dimethylformamide (DMF), and 113 g of ISOPAR-G as in Example 1 were placed in a 00 ml four-necked flask at room temperature. However, no fever was observed. Stirring was started, and the reaction was carried out while heating and refluxing at 105° C. for 3 hours. Then, the cooling tube was replaced with a water quantitative receiver equipped with a cooling tube at the top similar to that in Example 1, and after heating to 160°C, the reaction was continued at that temperature until the concentration of hydrazine became 1% or less. . The reaction time at 160°C was 8 hours.

【0021】反応終了後、100℃まで冷却し、分液に
より下層の目的物を分別した。若干ISOPAR−Gが
含まれているため、ISOPAR−Gを減圧下に除去し
た。目的物が53.6g(粗収率95.7%)得られ、
純度は93.0%であった。
After the reaction was completed, the mixture was cooled to 100° C. and the target product in the lower layer was separated by liquid separation. Since some ISOPAR-G was contained, ISOPAR-G was removed under reduced pressure. 53.6g (crude yield 95.7%) of the target product was obtained,
Purity was 93.0%.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  蟻酸、そのエステル類又はアミド類と
ヒドラジンとを加熱下に反応させて4−アミノ−1,2
,4−トリアゾールを製造する方法において、有機溶媒
の存在下に反応を行なうことを特徴とする4−アミノ−
1,2,4−トリアゾールの製法。
Claim 1: Formic acid, its esters or amides are reacted with hydrazine under heating to produce 4-amino-1,2
, 4-triazole, characterized in that the reaction is carried out in the presence of an organic solvent.
Method for producing 1,2,4-triazole.
JP15082391A 1991-04-04 1991-04-04 Production of 4-amino-1,2,4-triazole Pending JPH04308582A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15082391A JPH04308582A (en) 1991-04-04 1991-04-04 Production of 4-amino-1,2,4-triazole

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15082391A JPH04308582A (en) 1991-04-04 1991-04-04 Production of 4-amino-1,2,4-triazole

Publications (1)

Publication Number Publication Date
JPH04308582A true JPH04308582A (en) 1992-10-30

Family

ID=15505187

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15082391A Pending JPH04308582A (en) 1991-04-04 1991-04-04 Production of 4-amino-1,2,4-triazole

Country Status (1)

Country Link
JP (1) JPH04308582A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6504033B1 (en) 1996-11-07 2003-01-07 Elf Atochem S.A. Process for the preparation of 4-amino-1,2,4-Triazole

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6504033B1 (en) 1996-11-07 2003-01-07 Elf Atochem S.A. Process for the preparation of 4-amino-1,2,4-Triazole

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