JPH05247004A - Synthesis of 3-amino-5-mercapto-1,2,4-triazole - Google Patents

Synthesis of 3-amino-5-mercapto-1,2,4-triazole

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Publication number
JPH05247004A
JPH05247004A JP21322391A JP21322391A JPH05247004A JP H05247004 A JPH05247004 A JP H05247004A JP 21322391 A JP21322391 A JP 21322391A JP 21322391 A JP21322391 A JP 21322391A JP H05247004 A JPH05247004 A JP H05247004A
Authority
JP
Japan
Prior art keywords
reaction
thiocyanate
aminoguanidine
asta
acid salt
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.)
Granted
Application number
JP21322391A
Other languages
Japanese (ja)
Other versions
JP2959883B2 (en
Inventor
Takehiko Yoshie
武彦 吉江
Masanori Sasaki
正典 佐々木
Masahiko Yoshida
昌彦 吉田
Hiroshi Shibabuchi
弘 芝淵
Yasushi Imai
靖志 今井
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 Carbide Industries Co Inc
Original Assignee
Nippon Carbide Industries Co Inc
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Filing date
Publication date
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Priority to JP21322391A priority Critical patent/JP2959883B2/en
Publication of JPH05247004A publication Critical patent/JPH05247004A/en
Application granted granted Critical
Publication of JP2959883B2 publication Critical patent/JP2959883B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To safely and inexpensively obtain 3-methyl-5-mercapto-1,2,4-triazole useful as an intermediate for medicines and agricultural chemical materials in easy operation and high yield. CONSTITUTION:(i) >=0.5mol, especially 0.5-2mol thiocyanic acid salt, particularly ammonium thiocyanate based on 1mol aminoguanidine thiocyanic acid salt of formula I is added to the compound of formula I and both components are subjected to heat reaction, normally in solventless and melted conditions, normally at >=130 deg.C, especially at 150-190 deg.C or (ii) the amino guanidine salt and normally 1-20mol, preferably 1-5mol thiocyanic acid salt based on 1mol of the compound are subjected to heat melt reaction, preferably under solventless condition at the above-mentioned temperature condition to advantageously provide the objective compound of formula II. According to the method, problems of a conventional method, e.g. toxicity and danger of raw material, increased cost of production equipment accompanied thereby and insufficient reaction yield can be solved and further, lowering of reaction rate by increase of viscosity of reaction system can be suppressed by use of thiocyanic acid salt.

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、医薬および農薬材料の
中間原料として有用な3-メチル-5-メルカプト-1,2,4-ト
リアゾールの合成法に関するものであり、詳しくは、チ
オシアン酸アミノグアニジンを加熱反応させることを特
徴とする3-アミノ-5-メルカプト-1,2,4-トリアゾールの
合成法に関し、特には、アミノグアニジン塩とチオシア
ン酸塩とを反応させることを特徴とする3-アミノ-5-メ
ルカプト-1,2,4-トリアゾールの合成法に関するもので
ある。
FIELD OF THE INVENTION The present invention relates to a method for synthesizing 3-methyl-5-mercapto-1,2,4-triazole which is useful as an intermediate raw material for pharmaceuticals and agricultural chemicals. A method for synthesizing 3-amino-5-mercapto-1,2,4-triazole, which is characterized by reacting guanidine with heating, and is particularly characterized by reacting an aminoguanidine salt with a thiocyanate salt. The present invention relates to a method for synthesizing -amino-5-mercapto-1,2,4-triazole.

【0002】[0002]

【従来の技術】3-アミノ-5-メルカプト-1,2,4-トリア
ゾール(以下、ASTAと略記することがある)の合成法に
ついては、従来いくつかの方法が知られており、例えば
西独国公開特許第1960981号公報には、先ず、酢酸を溶
解したエタール中に重炭酸アミノグアニジンを溶解さ
せ、これにトリエチルアミンを加えた後、二硫化炭素を
吹きこんで反応させる方法が提案されている。この反応
は、次式(イ)〜(ハ)に従うものと考えられる。
2. Description of the Related Art There are several conventionally known methods for synthesizing 3-amino-5-mercapto-1,2,4-triazole (hereinafter sometimes abbreviated as ASTA), such as West Germany. Japanese Patent Publication No. 1960981 proposes a method in which aminoguanidine bicarbonate is first dissolved in acetal-dissolved etal, triethylamine is added thereto, and then carbon disulfide is blown in to react. . This reaction is considered to follow the following equations (a) to (c).

【0003】[0003]

【化1】 [Chemical 1]

【0004】[0004]

【化2】 [Chemical 2]

【0005】[0005]

【化3】 [Chemical 3]

【0006】また、ソ連特許第1002291号公報には、次
式(ニ)で示すように塩酸アミノグアニジンとチオ尿素と
を無溶媒下に熔融反応させて合成する方法が提案されて
いる。
[0006] Also, USSR Patent No. 1002291 proposes a method of synthesizing aminoguanidine hydrochloride and thiourea by melting reaction in the absence of solvent as shown in the following formula (D).

【0007】[0007]

【化4】 [Chemical 4]

【0008】しかしながら、本発明方法である、チオシ
アン酸アミノグアニジンを加熱反応さる方法やアミノグ
アニジン塩とチオシアン酸塩とを反応させる方法は知ら
れていない。
However, the method of heating the aminoguanidine thiocyanate and the method of reacting the aminoguanidine salt with the thiocyanate, which are the methods of the present invention, are not known.

【0009】そして、前記第1の提案の方法では、原料
の二硫化炭素の毒性や引火・爆発性などの問題点があ
り、装置の密閉性、排気・排水などの処理設備などに格
別な注意を要し、コスト高となることを免れえず、ま
た、前記第2の提案の方法では、反応収率が必ずしも十
分とはいえない上、原料のチオ尿素は毒性や発癌性が問
題となっており、前記第1の提案と同様に製造設備上コ
スト高となるなどの問題があることがわかった。
In the method of the first proposal, there are problems such as toxicity of carbon disulfide as a raw material, flammability and explosiveness, and special attention should be paid to the equipment's hermeticity and treatment facilities such as exhaust and drainage. However, in the method of the second proposal, the reaction yield is not always sufficient, and thiourea as a raw material has problems of toxicity and carcinogenicity. Therefore, it has been found that there is a problem that the cost is increased due to the manufacturing facility as in the case of the first proposal.

【0010】[0010]

【発明の解決しようとする問題点】本発明者等は、従来
技術が有していた前述の問題点を解消し、安全で安価な
ASTAの合成法を開発すべく研究を進めた結果、例えば、
重炭酸アミノグアニジンなどのアミノグアニジン塩とチ
オシアン酸アンモニウムなどのチオシアン酸塩とを無溶
媒下に加熱反応させることにより、容易且つ安全に目的
のASTAを合成できることを見出し、さらに研究を進めて
本発明を完成した。
DISCLOSURE OF THE INVENTION The inventors of the present invention have solved the above-mentioned problems of the prior art and are safe and inexpensive.
As a result of conducting research to develop a synthetic method of ASTA, for example,
It was found that the target ASTA can be easily and safely synthesized by heating and reacting an aminoguanidine salt such as aminoguanidine bicarbonate with a thiocyanate such as ammonium thiocyanate in a solvent-free manner, and further research is conducted to further the present invention. Was completed.

【0011】[0011]

【問題点を解決するための手段】本発明は、チオシアン
酸アミノグアニジンを加熱反応させることを特徴とする
3-アミノ-5-メルカプト-1,2,4-トリアゾールの合成法の
提供を目的とするものであり、また、アミノグアニジン
塩とチオシアン酸塩とを反応させることを特徴とする3-
アミノ-5-メルカプト-1,2,4-トリアゾールの合成法の提
供を目的とするものである。
The present invention is characterized in that aminoguanidine thiocyanate is reacted by heating.
It is intended to provide a method for synthesizing 3-amino-5-mercapto-1,2,4-triazole, which is characterized by reacting an aminoguanidine salt with a thiocyanate salt.
It is intended to provide a method for synthesizing amino-5-mercapto-1,2,4-triazole.

【0012】以下本発明を詳細に説明する。本発明は、
まず、チオシアン酸アミノグアニジンを加熱反応させる
ことを特徴とするASTAの合成法である。
The present invention will be described in detail below. The present invention is
First, the method for synthesizing ASTA is characterized by reacting aminoguanidine thiocyanate with heat.

【0013】この反応は、次式(1)のように進行するも
のと考えられる。
This reaction is considered to proceed as in the following equation (1).

【0014】[0014]

【化5】 [Chemical 5]

【0015】上記の反応は、通常、実質的に無溶媒・熔
融状態で進行し、次第に反応系粘度が上昇して反応速度
が低下する傾向がある。このため、反応系粘度の上昇を
押さえる目的で、後記するチオシアン酸塩を、原料チオ
シアン酸アミノグアニジン1モルに対して0.5モル以
上、特には0.5〜2モル添加するのが好ましい。
The above reaction usually proceeds in a substantially solvent-free and molten state, and the viscosity of the reaction system gradually increases and the reaction rate tends to decrease. Therefore, for the purpose of suppressing an increase in the viscosity of the reaction system, it is preferable to add the thiocyanate described below in an amount of 0.5 mol or more, particularly 0.5 to 2 mol, based on 1 mol of aminoguanidine thiocyanate as a raw material.

【0016】反応温度は一般に130℃以上で行うことが
できるが、反応速度、原料や生成したASTAの分解および
副反応の抑制等の観点から150℃〜190℃が最も好まし
い。
The reaction temperature can be generally 130.degree. C. or higher, but 150.degree. C. to 190.degree. C. is most preferable from the viewpoints of reaction rate, decomposition of raw materials and produced ASTA and suppression of side reactions.

【0017】反応時間は、特に制限されるものではない
が、一般に15分〜64時間、好ましくは、14〜20時間の範
囲で行うのがよい。
The reaction time is not particularly limited, but it is generally 15 minutes to 64 hours, preferably 14 to 20 hours.

【0018】本発明の原料であるチオシアン酸アミノグ
アニジンは、例えば、アミノグアニジン塩とチオシアン
酸塩とを反応させることにより得ることができる。
The aminoguanidine thiocyanate, which is the raw material of the present invention, can be obtained, for example, by reacting an aminoguanidine salt with a thiocyanate.

【0019】上記のアミノグアニジン塩としては、例え
ば、塩酸アミノグアニジン、二塩酸アミノグアニジン、
硫酸アミノグアニジン、重硫酸アミノグアニジン、炭酸
アミノグアニジン、重炭酸アミノグアニジンなどを挙げ
ることができ、これらのうち、工業的スケールで反応を
行った場合の操作性のよさ、入手の容易さなどの観点か
ら重炭酸アミノグアニジンの使用が最も好ましい。
Examples of the above aminoguanidine salts include aminoguanidine hydrochloride, aminoguanidine dihydrochloride,
Examples thereof include aminoguanidine sulfate, aminoguanidine bisulfate, aminoguanidine carbonate, aminoguanidine bicarbonate, and the like. Among these, operability in the case of carrying out the reaction on an industrial scale, easy availability, etc. Most preferred is the use of aminoguanidine bicarbonate.

【0020】また、前記チオシアン酸塩としては、例え
ば、チオシアン酸アンモニウム、チオシアン酸カリウ
ム、チオシアン酸ナトリウム、チオシアン酸リチウム、
チオシアン酸カルシウム、チオシアン酸マグネシウム、
チオシアン酸バリウムなどを挙げることができ、これら
のうち、工業的スケールで反応を行った場合の操作性の
よさ、入手の容易さなどの観点からチオシアン酸アンモ
ニウムの使用が最も好ましい。
Examples of the thiocyanates include ammonium thiocyanate, potassium thiocyanate, sodium thiocyanate, lithium thiocyanate,
Calcium thiocyanate, magnesium thiocyanate,
Examples thereof include barium thiocyanate, and of these, ammonium thiocyanate is most preferable from the viewpoints of operability when the reaction is carried out on an industrial scale and easy availability.

【0021】チオシアン酸アミノグアニジンの生成反応
は、アミノグアニジン塩として重炭酸グアニジン、チオ
シアン酸塩としてチオシアン酸アンモニウムを用いた場
合、次式(2)に従うものと考えられる。
The formation reaction of aminoguanidine thiocyanate is considered to follow the following formula (2) when guanidine bicarbonate as the aminoguanidine salt and ammonium thiocyanate as the thiocyanate are used.

【0022】[0022]

【化6】 [Chemical 6]

【0023】さらに本発明においては、アミノグアニジ
ン塩とチオシアン酸塩とを、好ましくは無溶媒下、加熱
熔融反応させて、3-アミノ-5-メルカプト-1,2,4-トリア
ゾールを合成することもできる。この反応も、反応中間
体としてチオシアン酸アミノグアニジンを経由している
が、該チオシアン酸アミノグアニジンを単離することな
くそのまま加熱反応を継続することによって、目的化合
物である3-アミノ-5-メルカプト-1,2,4-トリアゾールを
合成することができる。
Further, in the present invention, the aminoguanidine salt and the thiocyanate salt are subjected to a melting reaction under heating, preferably in the absence of a solvent, to synthesize 3-amino-5-mercapto-1,2,4-triazole. You can also This reaction also passes through aminoguanidine thiocyanate as a reaction intermediate, but by continuing the heating reaction as it is without isolating the aminoguanidine thiocyanate, the target compound 3-amino-5-mercapto is obtained. -1,2,4-triazole can be synthesized.

【0024】アミノグアニジン塩として重炭酸アミノグ
アニジンを用い、チオシアン酸塩としてチオシアン酸ア
ンモニウムを用いたときの反応は、次式(3)にしたがっ
て進行するものと考えられる。
The reaction when aminoguanidine bicarbonate is used as the aminoguanidine salt and ammonium thiocyanate is used as the thiocyanate is considered to proceed according to the following formula (3).

【0025】[0025]

【化7】 [Chemical 7]

【0026】本発明の上記の反応もまた、通常、実質的
に無溶媒・熔融状態で進行する。この反応において、前
記チオシアン酸塩の使用量は、理論上は、アミノグアニ
ジン塩1モルに対して1モルであるが、通常、1モル〜
20モル、好ましくは、1モル〜5モル、特に好ましく
は、1.5モル〜3モルである。該チオシアン酸塩の使用
量が該下限値以上であれば、反応系粘度が高くなり過ぎ
たり、固化してしまったりすることがなく、反応性や攪
拌性が悪くなることがないので好ましく、一方、該上限
値以下であれば、後記する目的化合物ASTA精製時の濾別
に際しても操作性の低下がなく、また、経済性にも優れ
ているので好ましい。
The above reaction of the present invention also usually proceeds in a substantially solvent-free and molten state. In this reaction, the amount of the thiocyanate used is theoretically 1 mol with respect to 1 mol of the aminoguanidine salt, but usually 1 mol-
20 mol, preferably 1 mol to 5 mol, particularly preferably 1.5 mol to 3 mol. When the amount of the thiocyanate used is at least the lower limit value, the reaction system viscosity does not become too high or solidify, and the reactivity and stirring property do not deteriorate, which is preferable. If it is at most the upper limit value, the operability will not be deteriorated even during filtration when purifying the target compound ASTA, which will be described later, and the economy will be excellent, which is preferable.

【0027】反応温度は一般に130℃以上で行うことが
できるが、反応速度、原料や生成したASTAの分解および
副反応の抑制等の観点から150℃〜190℃が最も好まし
い。
The reaction temperature can be generally 130 ° C. or higher, but 150 ° C. to 190 ° C. is most preferable from the viewpoints of reaction rate, decomposition of raw materials and produced ASTA, and suppression of side reactions.

【0028】反応時間は、特に制限されるものではない
が、一般に15分〜64時間、好ましくは、14〜20時間の範
囲で行うのがよい。
The reaction time is not particularly limited, but it is generally 15 minutes to 64 hours, preferably 14 to 20 hours.

【0029】なお、原料の仕込みについては、チオシア
ン酸塩とアミノグアニジン塩のみを仕込み反応を行って
もかまわないが、操作および反応初期の攪拌を考慮する
と、チオシアン酸塩の仕込みに際して、若干の水、メタ
ノール、エタノール、アセトンなどを加え操作性を良く
してもよい。
Regarding the charging of the raw materials, the reaction may be carried out by charging only thiocyanate and aminoguanidine salt, but considering the operation and stirring at the initial stage of the reaction, a slight amount of water may be added when the thiocyanate is charged. The operability may be improved by adding methanol, ethanol, acetone or the like.

【0030】このようにして本発明の目的化合物である
ASTAが得られるが、さらに高純度のものが得たい場合に
は、カラムクロマトグラフィー、酸析などの方法を用い
て精製することがることができる。
Thus, the target compound of the present invention is obtained.
ASTA can be obtained, but if a higher purity is desired, it can be purified using a method such as column chromatography or acid precipitation.

【0031】酸析としては、反応で得られたASTAを含む
反応混合物に水を添加してスラリー溶液とし、吸引濾過
によりASTAと残留原料のチオシアン酸塩を溶解している
濾液とを濾別し、さらにこのASTAを、一旦、水酸化ナト
リウムなどのアルカリ金属水酸化物水溶液に溶解させて
ASTAのアルカリ金属塩の水溶液とし、吸引濾過によりイ
オウ分などの不溶分を濾別する。そして、そのASTAアル
カリ金属塩の水溶液に塩酸などの無機酸を加えpH1〜2
にして、析出したASTAを吸引濾過により濾別して乾燥す
ることにより95〜99%のASTA結晶を得ることができる。
For the acid precipitation, water is added to the reaction mixture containing ASTA obtained in the reaction to form a slurry solution, and ASTA and the filtrate in which the residual raw material thiocyanate is dissolved are filtered off by suction filtration. , Furthermore, once dissolve this ASTA in an aqueous solution of alkali metal hydroxide such as sodium hydroxide.
An aqueous solution of ASTA alkali metal salt is prepared, and insoluble matter such as sulfur is filtered off by suction filtration. Then, add an inorganic acid such as hydrochloric acid to the aqueous solution of the ASTA alkali metal salt to adjust the pH to 1-2.
Then, 95% to 99% of ASTA crystals can be obtained by separating the precipitated ASTA by suction filtration and drying.

【0032】[0032]

【実施例】以下実施例により本発明を具体的に説明する
が、本発明は、これに限定されるものではない。
EXAMPLES The present invention will be specifically described below with reference to examples, but the present invention is not limited thereto.

【0033】実施例1 温度計、攪拌装置を供えた100mlの三角フラスコに重炭
酸アミノグアニジン20.8g(0.15モル)、チオシアン酸ア
ンモニウム22.3g(0.30モル)を仕込み、オイルバス上で
加熱して熔融させ、攪拌しながら、150℃、16時間反応
させた。反応終了後、反応混合物に水31.4g及び35重量
%塩酸水溶液0.49gを添加し、室温に冷却後、生成して
いるASTAの沈殿を吸引濾過し、含水ASTA 15.7gを得た。
Example 1 A 100 ml Erlenmeyer flask equipped with a thermometer and a stirrer was charged with 20.8 g (0.15 mol) of aminoguanidine bicarbonate and 22.3 g (0.30 mol) of ammonium thiocyanate and heated on an oil bath to melt. The mixture was allowed to react with stirring at 150 ° C. for 16 hours. After completion of the reaction, 31.4 g of water and 0.49 g of 35 wt% hydrochloric acid aqueous solution were added to the reaction mixture, and after cooling to room temperature, the formed ASTA precipitate was suction filtered to obtain 15.7 g of water-containing ASTA.

【0034】次にこのASTAを10重量%水酸化ナトリウム
水溶液58.9gに溶解させ、不溶分を吸引濾過により濾別
し、ASTAの水酸化ナトリウム水溶液75.7gを得た。これ
にpHが1〜2になるように35重量%塩酸水溶液16.8gを
加えてASTAを酸析させ、吸引濾過で濾別し、含水ASTA 1
7.4gを得た。これを80℃で1晩減圧乾燥させ、純度97.2
重量%のASTA結晶11.6g(収率64.9%)を得た。得られた
ASTAの融点は300〜302℃であり、標品と一致した。
Next, this ASTA was dissolved in 58.9 g of a 10% by weight aqueous sodium hydroxide solution, and the insoluble matter was filtered off by suction filtration to obtain 75.7 g of an aqueous sodium hydroxide solution of ASTA. To this, 16.8 g of 35 wt% hydrochloric acid aqueous solution was added to adjust pH to 1-2, ASTA was acid-deposited, and filtered by suction filtration.
7.4 g was obtained. This was dried under reduced pressure at 80 ° C overnight to obtain a purity of 97.2
11.6 g (yield 64.9%) of ASTA crystals with a weight% was obtained. Got
The melting point of ASTA was 300 to 302 ° C, which was in agreement with the standard product.

【0035】実施例2 実施例1において、チオシアン酸アンモニウムを22.3g
(0.30モル)用いる代わりに、34.0g(0.45モル)用いる以
外は実施例1とほぼ同様に反応および精製を行い、純度
96.3重量%のASTA結晶12.5g(収率68.9%)を得た。得
られたASTAの融点は300〜301℃であり、標品と一致し
た。
Example 2 In Example 1, 22.3 g of ammonium thiocyanate was added.
Instead of using (0.30 mol), the reaction and purification were performed in substantially the same manner as in Example 1 except that 34.0 g (0.45 mol) was used, and the purity was
12.5 g (yield 68.9%) of ASTA crystals of 96.3% by weight was obtained. The melting point of the obtained ASTA was 300 to 301 ° C, which was in agreement with the authentic sample.

【0036】実施例3 300mlのナス型フラスコに重炭酸アミノグアニジン69.2g
(0.5モル)、水50g及びチオシアン酸アンモニウム38.3g
(0.5モル)を入れ、エバポレーターで減圧下、90〜100℃
で二酸化炭素、水及びアンモニアを除去して、97.1重量
%のチオシアン酸アミノグアニジン68.5g(0.5モル)を得
た。
Example 3 69.2 g of aminoguanidine bicarbonate in a 300 ml eggplant-shaped flask
(0.5 mol), water 50 g and ammonium thiocyanate 38.3 g
(0.5 mol) and put it under reduced pressure with an evaporator at 90-100 ° C.
The carbon dioxide, water and ammonia were removed with to obtain 68.5 g (0.5 mol) of 97.1 wt% aminoguanidine thiocyanate.

【0037】次に、実施例1で用いたと同様の装置に、
得られたチオシアン酸アミノグアニジン20.0g(0.15モ
ル)とチオシアン酸アンモニウム23.0g(0.30モル)を仕込
み、以下、実施例1とほぼ同様に反応および精製を行っ
て、純度95.8重量%のASTA結晶11.4g(収率62.8%)を
得た。得られたASTAの融点は299.5〜302℃であり、標品
と一致した。
Next, in the same apparatus as used in Example 1,
The obtained aminoguanidine thiocyanate (20.0 g, 0.15 mol) and ammonium thiocyanate (23.0 g, 0.30 mol) were charged, and the reaction and purification were carried out in the same manner as in Example 1 to obtain ASTA crystals 11.4 having a purity of 95.8% by weight. g (yield 62.8%) was obtained. The melting point of the obtained ASTA was 299.5 to 302 ° C, which was in agreement with the standard product.

【0038】なお、この実施例3におけるチオシアン酸
アンモニウムは、反応の熔融媒体として作用し、その使
用量を減らすと加熱反応時の反応系粘度が上昇し、ASTA
の収率も減少することがわかった。
The ammonium thiocyanate in Example 3 acts as a melting medium in the reaction, and if the amount used is reduced, the viscosity of the reaction system during the heating reaction increases, and ASTA
It was also found that the yield of H.

【0039】[0039]

【発明の効果】本発明方法は、従来法では用いられたこ
とのない原料であるチオシアン酸アミノグアニジンを用
い、あるいは、従来法にはない原料の組合せである、重
炭酸アミノグアニジンなどのアミノグアニジン塩と、チ
オシアン酸アンモニウムなどのチオシアン酸塩とを用い
るものであり、この方法によれば、従来法における各種
の問題点、すなわち、用いる原料の毒性や危険性、これ
に伴う製造設備などのコスト高および反応収率の不十分
さなどの問題点を解消して、安価に且つ安全に目的化合
物である3-アミノ-5-メルカプト-1,2,4-トリアゾールを
得ることができる。
INDUSTRIAL APPLICABILITY The method of the present invention uses aminoguanidine thiocyanate, which is a raw material that has not been used in the conventional method, or a combination of raw materials, which is not in the conventional method, such as aminoguanidine bicarbonate. A salt and a thiocyanate such as ammonium thiocyanate are used. According to this method, various problems in the conventional method, that is, toxicity and danger of raw materials used, cost of manufacturing equipment accompanying this, etc. It is possible to solve the problems such as high and insufficient reaction yield, and inexpensively and safely obtain the target compound 3-amino-5-mercapto-1,2,4-triazole.

【0040】特に、チオシアン酸アミノグアニジンの加
熱反応に際してチオシアン酸塩を添加併用し、あるい
は、アミノグアニジン塩とチオシアン酸塩との反応に際
し、アミノグアニジン塩に対して、チオシアン酸塩を過
剰に使用することにより、収率の向上および反応系の過
度の粘度上昇や固化などの防止という効果も認められ
る。
In particular, a thiocyanate is added and used in the heating reaction of aminoguanidine thiocyanate, or a thiocyanate is excessively used with respect to the aminoguanidine salt in the reaction of the aminoguanidine salt and the thiocyanate. As a result, the effects of improving the yield and preventing the viscosity of the reaction system from rising excessively and solidifying are recognized.

─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成4年10月23日[Submission date] October 23, 1992

【手続補正1】[Procedure Amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0005[Correction target item name] 0005

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0005】[0005]

【化3】 [Chemical 3]

【手続補正2】[Procedure Amendment 2]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0007[Correction target item name] 0007

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0007】[0007]

【化4】 [Chemical 4]

【手続補正3】[Procedure 3]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0014[Correction target item name] 0014

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0014】[0014]

【化5】 [Chemical 5]

【手続補正4】[Procedure amendment 4]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0025[Name of item to be corrected] 0025

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0025】[0025]

【化7】 [Chemical 7]

【手続補正5】[Procedure Amendment 5]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0034[Correction target item name] 0034

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0034】次にこのASTAを10重量%水酸化ナトリウム
水溶液58.9gに溶解させ、不溶分を吸引濾過により濾別
し、ASTAの水酸化ナトリウム水溶液75.7gを得た。これ
にpHが1〜2になるように35重量%塩酸水溶液16.8gを
加えてASTAを酸析させ、吸引濾過で濾別し、含水ASTA 1
7.4gを得た。これを80℃で1晩減圧乾燥させ、純度97.2
重量%のASTA結晶11.6g(収率64.9%)を得た。得られた
ASTAの分解点は300〜302℃であり、標品と一致した。
Next, this ASTA was dissolved in 58.9 g of a 10% by weight aqueous sodium hydroxide solution, and the insoluble matter was filtered off by suction filtration to obtain 75.7 g of an aqueous sodium hydroxide solution of ASTA. To this, 16.8 g of 35 wt% hydrochloric acid aqueous solution was added to adjust the pH to 1-2, ASTA was acid-deposited, and filtered by suction filtration to obtain water-containing ASTA 1
7.4 g was obtained. This was dried under reduced pressure at 80 ° C overnight to obtain a purity of 97.2
11.6 g (yield 64.9%) of ASTA crystals with a weight% was obtained. Got
The decomposition point of ASTA was 300-302 ℃, which was in agreement with the standard product.

【手続補正6】[Procedure correction 6]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0035[Correction target item name] 0035

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0035】実施例2 実施例1において、チオシアン酸アンモニウムを22.3g
(0.30モル)用いる代わりに、34.0g(0.45モル)用いる以
外は実施例1とほぼ同様に反応および精製を行い、純度
96.3重量%のASTA結晶12.5g(収率68.9%)を得た。得
られたASTAの分解点は300〜301℃であり、標品と一致し
た。
Example 2 In Example 1, 22.3 g of ammonium thiocyanate was added.
Instead of using (0.30 mol), the reaction and purification were performed in substantially the same manner as in Example 1 except that 34.0 g (0.45 mol) was used, and the purity was
12.5 g (yield 68.9%) of ASTA crystals of 96.3% by weight was obtained. The decomposition point of the obtained ASTA was 300-301 ° C, which was in agreement with the standard product.

【手続補正7】[Procedure Amendment 7]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0037[Name of item to be corrected] 0037

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0037】次に、実施例1で用いたと同様の装置に、
得られたチオシアン酸アミノグアニジン20.0g(0.15モ
ル)とチオシアン酸アンモニウム23.0g(0.30モル)を仕込
み、以下、実施例1とほぼ同様に反応および精製を行っ
て、純度95.8重量%のASTA結晶11.4g(収率62.8%)を
得た。得られたASTAの分解点は299.5〜302℃であり、標
品と一致した。
Next, in the same apparatus as used in Example 1,
The obtained aminoguanidine thiocyanate (20.0 g, 0.15 mol) and ammonium thiocyanate (23.0 g, 0.30 mol) were charged, and the reaction and purification were carried out in the same manner as in Example 1 to obtain ASTA crystals 11.4 having a purity of 95.8% by weight. g (yield 62.8%) was obtained. The decomposition point of the obtained ASTA was 299.5 to 302 ° C, which was in agreement with the standard product.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 今井 靖志 神奈川県平塚市見附町46−31 ライオンズ マンション平塚見附町第2 213号 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Yasushi Imai 46-31 Mitsuke-cho, Hiratsuka-shi, Kanagawa Lions Mansion Hiratsuka-Mitsuke-cho No. 2213

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 チオシアン酸アミノグアニジンを加熱反
応させることを特徴とする3-アミノ-5-メルカプト-1,2,
4-トリアゾールの合成法。
1. 3-Amino-5-mercapto-1,2, characterized by reacting aminoguanidine thiocyanate with heat.
Synthesis of 4-triazole.
【請求項2】 アミノグアニジン塩とチオシアン酸塩と
を反応させることを特徴とする3-アミノ-5-メルカプト-
1,2,4-トリアゾールの合成法。
2. An aminoguanidine salt and a thiocyanate are reacted with each other, 3-amino-5-mercapto-
Synthesis of 1,2,4-triazole.
JP21322391A 1991-07-31 1991-07-31 Method for synthesizing 3-amino-5-mercapto-1,2,4-triazole Expired - Fee Related JP2959883B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21322391A JP2959883B2 (en) 1991-07-31 1991-07-31 Method for synthesizing 3-amino-5-mercapto-1,2,4-triazole

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21322391A JP2959883B2 (en) 1991-07-31 1991-07-31 Method for synthesizing 3-amino-5-mercapto-1,2,4-triazole

Publications (2)

Publication Number Publication Date
JPH05247004A true JPH05247004A (en) 1993-09-24
JP2959883B2 JP2959883B2 (en) 1999-10-06

Family

ID=16635577

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Country Status (1)

Country Link
JP (1) JP2959883B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5559243A (en) * 1994-12-13 1996-09-24 Nippon Carbide Kogyo Kabushiki Kaisha Processes for producing a salt of N-guanidino thiourea and 3-amino-5-mercapto-1,2,4-triazole

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5559243A (en) * 1994-12-13 1996-09-24 Nippon Carbide Kogyo Kabushiki Kaisha Processes for producing a salt of N-guanidino thiourea and 3-amino-5-mercapto-1,2,4-triazole
US5714617A (en) * 1994-12-13 1998-02-03 Nippon Carbide Kogyo Kabushiki Kaisha Processes for producing a salt of N-guanidino thiourea and 3-amino-5-mercapto-1,2,4-triazole

Also Published As

Publication number Publication date
JP2959883B2 (en) 1999-10-06

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