JPS5929657A - Preparation of beta-mercaptopropionitrile - Google Patents

Preparation of beta-mercaptopropionitrile

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Publication number
JPS5929657A
JPS5929657A JP13855782A JP13855782A JPS5929657A JP S5929657 A JPS5929657 A JP S5929657A JP 13855782 A JP13855782 A JP 13855782A JP 13855782 A JP13855782 A JP 13855782A JP S5929657 A JPS5929657 A JP S5929657A
Authority
JP
Japan
Prior art keywords
acid
chloropropionitrile
thiosulfate
beta
mercaptopropionitrile
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
JP13855782A
Other languages
Japanese (ja)
Other versions
JPS6318943B2 (en
Inventor
Tetsuro Nakahama
中浜 哲朗
Yasuyuki Takayanagi
高柳 恭之
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.)
Nitto Chemical Industry Co Ltd
Original Assignee
Nitto Chemical Industry 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 Nitto Chemical Industry Co Ltd filed Critical Nitto Chemical Industry Co Ltd
Priority to JP13855782A priority Critical patent/JPS5929657A/en
Publication of JPS5929657A publication Critical patent/JPS5929657A/en
Publication of JPS6318943B2 publication Critical patent/JPS6318943B2/ja
Granted legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PURPOSE:To prepare the titled compound useful as a synthetic raw material of organic chemicals such as pharmaceuticals, agricultural chemicals, etc. from inexpensive low-toxic raw materials, in high yield, by reacting beta-chloropropionnitrile with a thiosulfuric acid salt, and hydrolyzing the product in the presence of an acid. CONSTITUTION:beta-Chloropropionitrile is made to react with a thiosulfuric acid salt in an aqueous medium such as water, alcohol, dioxane, etc. at a temperature between 60 deg.C and the boiling point of the solvent for 15min-5hr to obtain Bunte salt, which can be converted to the objective compound by hydrolyzing at a temperature between 60 deg.C and the boiling point of the solvent for 30min-8hr in the presence of an acid such as sulfuric acid, hydrochloric acid, etc. The molar ratio of beta-chloropropionitrile:thiosulfate is 1:(0.8-1.2), and that of beta-chloropropionitrile: acid is 1:(0.5-5.0). The thiosulfuric acid salt is e.g. sodium thiosulfate, magnesium thiosulfate, ammonium thiosulfate, etc.

Description

【発明の詳細な説明】 本発明はβ−メルカプトプロピオニトリルの製造法に関
する。さらに具体的にはアクリロニトリルから容易に得
られるβ−クロロプロピオニトリルとチオ硫酸塩を原料
とするβ−メルカプトプロピオニトリルの製造法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing β-mercaptopropionitrile. More specifically, the present invention relates to a method for producing β-mercaptopropionitrile using β-chloropropionitrile and thiosulfate, which are easily obtained from acrylonitrile, as raw materials.

β−メルカプトプロピオニトリルは医薬、農薬をはじめ
とする多くの有機合成品の原料として有用な化合物であ
る。
β-Mercaptopropionitrile is a compound useful as a raw material for many organic synthetic products including medicines and agricultural chemicals.

β−メルカプトプロピオニトリルの製造法としては従来
種々の方法が知られている。
Various methods are conventionally known for producing β-mercaptopropionitrile.

代表的な製造法としてはβ−クロロプロピオニトリルあ
るいはアクリロニトリルとチオ尿素の反     ・応
により生成するイソチウロニウム塩をアルカリ加水分解
してβ−メルカプトプロピオニトリルを得る方法CJ、
Org、 Chem、 26 1443 (1961)
参照〕、またはβ−クロロプロピオニトリルと二硫化炭
素および水酸化ナトリウムとをインプロパツール中で反
応させて、生成するキサントゲン酸エステルを減圧下熱
分解する方法〔米国特許第3211777号明細書参照
〕、さらにはアクリロニトリルとチオ酢酸の反応で得ら
れるチオ酢酸エステルを加水分解する方法〔米国特許第
2630448号明細書参照〕ガどがある。
Typical production methods include the method of obtaining β-mercaptopropionitrile by alkaline hydrolysis of isothiuronium salt produced by the reaction of β-chloropropionitrile or acrylonitrile with thiourea CJ;
Org, Chem, 26 1443 (1961)
[see U.S. Pat. No. 3,211,777], or a method in which β-chloropropionitrile is reacted with carbon disulfide and sodium hydroxide in an inproper tool, and the resulting xanthate ester is thermally decomposed under reduced pressure [see U.S. Pat. No. 3,211,777] ], and a method of hydrolyzing a thioacetate obtained by the reaction of acrylonitrile and thioacetic acid [see US Pat. No. 2,630,448].

これらの方法によれば比較的容易にβ−メルカプトプロ
ピオニトリルを得ることができるが、副原料である硫黄
源化合物に毒性が強く取扱い難い二硫化炭素や工業原料
としては高価なチオ尿素あるいはチオ酢酸を用いるなど
の欠点を有し、必ずしも経済的な工業的製法とは言い難
い。
Although β-mercaptopropionitrile can be obtained relatively easily by these methods, the sulfur source compound used as an auxiliary raw material is carbon disulfide, which is highly toxic and difficult to handle, and thiourea or thiourea, which is expensive as an industrial raw material. It has drawbacks such as the use of acetic acid, and cannot necessarily be called an economical industrial production method.

一方、よシ安価な原料を使用する製造法としてはアクリ
ロニトリルと硫化水素の反応によシ直接β−メルカプト
プロピオニトリルを得る試みが提案されている。〔米国
特許第3280163号明細書および特公昭43−18
369号公報参照〕。しかしながら、これらの反応は副
生物のチオジプロピオニトリルの生成を避けるため大過
剰(3〜10)]′倍モル)の硫化水素を用い加圧下で
行なわれ、そのため反応装置は腐蝕性の非常に強い硫化
水素の高圧系に耐え得る特別な材質を選ぶ必要があシ。
On the other hand, as a production method using cheaper raw materials, an attempt has been proposed to directly obtain β-mercaptopropionitrile by reacting acrylonitrile with hydrogen sulfide. [U.S. Pat.
See Publication No. 369]. However, these reactions are carried out under pressure using a large excess (3 to 10 times molar) of hydrogen sulfide to avoid the formation of the by-product thiodipropionitrile, and the reactor is therefore highly corrosive. It is necessary to select a special material that can withstand the high pressure system of strong hydrogen sulfide.

工業的製法として非常に不利になる。This is extremely disadvantageous as an industrial manufacturing method.

このような状況の中で2本発明者らは繊維原料用などに
大量生産されているアクリロニトリルから安価に製造で
きるβ−クロロプロピオニトリルを主原料とし、しかも
安価で毒性の少ない硫黄源を用いるβ−メルカプトプロ
ピオニトリルの経済的な工業的製法を開発すべく鋭意研
究を行なった結果、硫黄源としてチオ硫酸塩を用いてβ
−メルカプトプロピオニトリルの前駆体としてBunt
e塩を生成させ1次いでこれを酸によシ加水分解するこ
とによシ高収率でβ−メルカプトプロピオニトリルが得
られることを見出して本発明に到達した。
Under these circumstances, the present inventors used β-chloropropionitrile, which can be produced inexpensively from acrylonitrile, which is mass-produced for textile raw materials, as the main raw material, and also used an inexpensive and less toxic sulfur source. As a result of intensive research to develop an economical industrial production method for β-mercaptopropionitrile, we found that β-mercaptopropionitrile was produced by using thiosulfate as a sulfur source.
- Bunt as a precursor of mercaptopropionitrile
The present invention has been accomplished by discovering that β-mercaptopropionitrile can be obtained in high yield by generating e-salt and then hydrolyzing it with acid.

すなわち2本発明は、水性媒体中でβ−クロロプロピオ
ニトリルをチオ硫酸塩と反応させることによシ、β−メ
ルカプトプロピオニトリルの前駆体として13unte
塩を生成せしめ2次いでとのBun−te塩を酸の存在
下で加水分解することを特徴とするβ−メルカプトプロ
ピオニトリルの製造法である。
That is, the present invention provides 13 unte as a precursor of β-mercaptopropionitrile by reacting β-chloropropionitrile with thiosulfate in an aqueous medium.
This is a method for producing β-mercaptopropionitrile, which is characterized by hydrolyzing Bun-te salt in the presence of an acid to form a salt.

本発明の反応を一般式で示すと次のようになる。The reaction of the present invention is expressed by the following general formula.

CI CHz CH2CN + Mvh Ss On→
Mvh03SICHxC’&CN +M171>CIM
vh 03 S2 CH2CH2CN 十Hz 0rH
8CHz CH2CN 十MVhH8O4〔ただし2M
はアルカリ金属、アルカリ土類金属またはアンモニウム
イオン、nはMの原子価またはイオン価で1または2で
ある。〕 本発明に用いる主原料のβ−クロロプロピオニ3− トリルは如何なる供給源から選ばれたものでもよい。β
−クロロプロピオニトリルをアクリロニトリルに対する
塩化水素の付加反応によって得る場合には、溶媒の存在
下または不存在下にアクリロニトリル中へ塩化水素ガス
を室温以下の温度に保ちながらボールフィルターなどを
通して導入することによすほぼ定量的に合成することが
できる。
CI CHz CH2CN + Mvh Ss On→
Mvh03SICHxC'&CN +M171>CIM
vh 03 S2 CH2CH2CN 10Hz 0rH
8CHZ CH2CN 10MVhH8O4 [However, 2M
is an alkali metal, alkaline earth metal or ammonium ion, and n is the valence or ionic valence of M and is 1 or 2. ] The main raw material β-chloropropioni-3-tolyl used in the present invention may be selected from any source. β
- When chloropropionitrile is obtained by the addition reaction of hydrogen chloride to acrylonitrile, hydrogen chloride gas is introduced into the acrylonitrile in the presence or absence of a solvent through a ball filter or the like while keeping the temperature below room temperature. It can be synthesized almost quantitatively.

また1本発明で用いるチオ硫酸塩はチオ硫酸ナトリウム
、チオ硫酸カリウムなどのチオ硫酸アルカリ金属塩、チ
オ硫酸マグネシウム、チオ硫酸カルシウムなどのチオ硫
酸アルカリ土類金属塩およびチオ硫酸アンモニウムなど
であシ、これらは1種類または2種類以上の混合物とし
て用いてもよい。チオ硫酸塩の結晶水の有無は何ら制限
はない。
In addition, the thiosulfates used in the present invention include alkali metal thiosulfates such as sodium thiosulfate and potassium thiosulfate, alkaline earth metal salts of thiosulfates such as magnesium thiosulfate and calcium thiosulfate, and ammonium thiosulfate. may be used alone or as a mixture of two or more. There is no restriction on the presence or absence of water of crystallization of thiosulfate.

これらのチオ硫酸塩の中では、大量に安価に工業生産さ
れているチオ硫酸ナトリウムの5水塩(通称「ハイポ」
)を用いるのが工業的製法には最も好ましい。
Among these thiosulfates, sodium thiosulfate pentahydrate (commonly known as "hypo") is industrially produced in large quantities at low cost.
) is most preferred for industrial production methods.

゛ 次に2本発明の一般的実施態様について説明する。Next, two general embodiments of the present invention will be described.

4− 1)  13unte塩の生成 β−クロロプロピオニトリルとチオ硫酸塩との反応によ
るBunte塩の生成は水性媒体中にてほぼ両者を等モ
ル用いて行なわれるが。
4-1) Production of 13unte salt The production of Bunte salt by the reaction of β-chloropropionitrile and thiosulfate is carried out in an aqueous medium using approximately equimolar amounts of both.

β−クロロプロピオニトリル:チオ硫酸塩=1:0.8
〜1.2(モル比) の範囲で、いずれか一方の原料を過剰に用いてもよい。
β-chloropropionitrile: thiosulfate = 1:0.8
-1.2 (molar ratio) You may use either raw material in excess.

水性媒体としては1例えば、水、または水−アルコール
、水−ジオキサン、水−テトラヒドロフランあるいは水
−ジネチルスルホキシドなどの混合液が用いられるが、
工業的には水または水−アルコール混合液中での反応が
有利である。
As the aqueous medium, for example, water or a mixed solution such as water-alcohol, water-dioxane, water-tetrahydrofuran, or water-dinethyl sulfoxide is used.
Industrially, the reaction in water or a water-alcohol mixture is advantageous.

水性媒体中のβ−クロロプロピオニトリルおよびチオ硫
酸塩の濃度はそれぞれ5.#〜50重量%程度とするの
が好ましいが、この場合必ずしも均一に混合している必
要はない。
The concentrations of β-chloropropionitrile and thiosulfate in the aqueous medium were 5. It is preferable that the amount is approximately 50% by weight, but in this case, it is not necessarily necessary to mix uniformly.

反応温度は通常60℃から反応液の沸点の範囲であシ、
また反応時間は15分から5時間程度で充分である。
The reaction temperature is usually in the range of 60°C to the boiling point of the reaction solution,
Further, a reaction time of about 15 minutes to 5 hours is sufficient.

反応後、得られたBunte塩は溶媒抽出などによシ無
機塩類と分離してから次の加水分解を行なってもよいが
9通常はそのまま引き続き酸を加えて加水分解を行なう
。13unte塩を単離する場合はアルコール類による
熱抽出などを用いることができる。
After the reaction, the Bunte salt obtained may be separated from the inorganic salts by solvent extraction or the like and then subjected to the next hydrolysis, 9 but usually, the hydrolysis is carried out by subsequently adding an acid. When 13unte salt is isolated, thermal extraction with alcohols or the like can be used.

2)加水分解 13unte塩の加水分解に用いる酸としては、塩酸、
硫酸、リン酸などの鉱酸類、ギ酸、シュウ酸などの有機
カルボン酸類、P−トルエンスルホン酸などの有機スル
ホン酸類、および強酸性イオン交換樹脂などの固体酸が
あるが2反応速度および反応後の分離工程などを勘案す
ると工業的には硫酸、塩酸などの鉱酸類が好ましい。
2) Hydrolysis The acids used for hydrolysis of 13unte salt include hydrochloric acid,
There are mineral acids such as sulfuric acid and phosphoric acid, organic carboxylic acids such as formic acid and oxalic acid, organic sulfonic acids such as P-toluenesulfonic acid, and solid acids such as strongly acidic ion exchange resins. Considering the separation process, etc., mineral acids such as sulfuric acid and hydrochloric acid are preferred from an industrial perspective.

使用する酸の量はβ−クロロプロピオニトリルを基準と
し。
The amount of acid used is based on β-chloropropionitrile.

β−クロロプロヒオニトリル:酸 =1:0.5〜3.0(モル比) 好ましくは。β-Chloroprohionitrile: acid =1:0.5-3.0 (molar ratio) Preferably.

β−クロロプロピオニトリル:酸 =1:1.O〜2.5(モル比) の範囲で選ばれる。β-chloropropionitrile: acid =1:1. O~2.5 (molar ratio) selected within the range.

酸の濃度は10〜40重量%の範囲が好ましい。The acid concentration is preferably in the range of 10 to 40% by weight.

加水分解反応の温度は通常60℃から反応液の沸点の範
囲であυ1反応時間は30分から8時間程度で充分であ
る。
The temperature of the hydrolysis reaction is usually in the range from 60°C to the boiling point of the reaction solution, and the reaction time υ1 is sufficient to be about 30 minutes to 8 hours.

なお、ここで例えば反応温度85℃以上で5時間以上反
応を行なうことによシ、得られたβ−メルカプトプロピ
オニトリルをさらにβ−メルカプトプロピオン酸に加水
分解できるため9条件を適当に選べばβ−クロロプロピ
オニトリルからβ−メルカプトプロピオン酸の一貫製造
が可能である。
Here, for example, by carrying out the reaction at a reaction temperature of 85°C or higher for 5 hours or more, the obtained β-mercaptopropionitrile can be further hydrolyzed to β-mercaptopropionic acid, so if the 9 conditions are appropriately selected, Integrated production of β-mercaptopropionic acid from β-chloropropionitrile is possible.

3)回収 反応終了後2反応混合物からのβ−メルカプトプロピオ
ニトリルの分離および精製は有機溶剤による抽出と抽出
液の蒸留によシ行なうことができる。抽出溶剤としては
β−メルカプトプロピオ 7− ニトリル 云檗を溶解し、しかも水と混和しないものであれば何で
も差し支えないが、特にベンゼン、トルエン、ジクロル
メタン、1,2−ジクロルエタン。
3) After the completion of the recovery reaction, β-mercaptopropionitrile can be separated and purified from the reaction mixture by extraction with an organic solvent and distillation of the extract. Any extraction solvent may be used as long as it dissolves β-mercaptopropio 7-nitrile and is immiscible with water, particularly benzene, toluene, dichloromethane, and 1,2-dichloroethane.

1 、 1 、  ] −) +J クロルエタン、ク
ロロホルムおよびエーテルなどが用いられる。
1 , 1 , ] −) +J Chlorethane, chloroform, ether, etc. are used.

以下、実施例によシ本発明をさらに具体的に説明するが
2本発明はこれら実施例に何ら限定されるものではない
Hereinafter, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited to these Examples in any way.

製造例〔β−クロロプロピオニトリルの製造〕撹拌機、
冷却コンデンサー、温度計およびガス導入管を付した反
応器に108.7fのアクリロニトリルを仕込み、水冷
して5℃に冷却後、ガス導入管から74.3tの塩化水
素を約7時間かけて導入した。塩化水素ガス導入中は反
応器内の液温は2〜6℃に保った。塩化水素導入終了後
、室温で2時間熟成し2次いで反応混合物を減圧蒸留し
たところ、x7xr(沸点94〜96℃/ff50kI
iTg、収率93E%、純度98%のβ−クロロプロピ
オニトリルが得られた。
Production example [Production of β-chloropropionitrile] Stirrer,
108.7 f of acrylonitrile was charged into a reactor equipped with a cooling condenser, a thermometer, and a gas inlet tube, and after cooling with water to 5°C, 74.3 tons of hydrogen chloride was introduced from the gas inlet tube over about 7 hours. . During the introduction of hydrogen chloride gas, the liquid temperature in the reactor was maintained at 2 to 6°C. After the introduction of hydrogen chloride, the reaction mixture was aged for 2 hours at room temperature and then distilled under reduced pressure.
β-chloropropionitrile with iTg, yield of 93E%, and purity of 98% was obtained.

実施例1 8− 1)  Bunte塩′の生成 温度計、攪拌機2滴下ロートおよび冷却コンデンサーを
付した反応器に250.8Fのチオ硫酸ナトリウム5水
塩と20ofの水を仕込み攪拌溶解させた。この溶液に
上記製造例に示したβ−クロロ7’oビオニトリル91
.6Fを2001のエタノールに溶かした溶液を滴下ロ
ートを通して添加し、還流下に5時間反応させた。
Example 1 8-1) Formation of Bunte's Salt In a reactor equipped with a thermometer, a stirrer, two dropping funnels, and a cooling condenser, 250.8 F sodium thiosulfate pentahydrate and 20 of water were charged and dissolved with stirring. Add β-chloro 7'o bionitrile 91 shown in the above production example to this solution.
.. A solution of 6F in 2001 ethanol was added through the dropping funnel and reacted under reflux for 5 hours.

次いで、減圧下に溶媒を留去し、若干含水したエタノー
ル600tで熱抽出した。得られた淡クリーム色の固体
をさらにエタノールから再結したところ153F(収率
81チ)の白色結晶状のBun−te塩が得られた。
Next, the solvent was distilled off under reduced pressure, and the mixture was extracted with heat using 600 tons of slightly water-containing ethanol. The obtained pale cream-colored solid was further reconsolidated from ethanol to obtain 153F (yield: 81%) of Bun-te salt in the form of white crystals.

生成物の元素分析値は第1表め通シであった。The elemental analysis values of the product were as shown in Table 1.

第1表 2)加水分解 このようにして得られたBunte塩481全4811
の水と752の36%塩酸の混合液に溶解して90℃で
1時間反応を行なったのち1反応液の一部を分取してガ
スクロマトグラフ分析を行なった結果、15.6F(反
応収率72チ)のβ−メルカプトプロピオニトリルの生
成を認めた。
Table 1 2) Hydrolysis Bunte salt thus obtained 481 total 4811
After dissolving 752 in a mixture of water and 36% hydrochloric acid and reacting at 90°C for 1 hour, a portion of the reaction solution was separated and analyzed by gas chromatography. As a result, the reaction yield was 15.6F. The production of β-mercaptopropionitrile at a rate of 72% was observed.

さらに9反応液を100−の1,2−ジクロルエタンで
抽出後、この抽出液を蒸留することによって14.2f
(沸点67〜b チ、純度99%)のβ−メルカプトプロピオニトリルが
得られた。
Furthermore, 9 reaction liquids were extracted with 100-1,2-dichloroethane, and this extract was distilled to yield 14.2f.
β-mercaptopropionitrile (boiling point 67-b, purity 99%) was obtained.

参考例1 実施例1の1)、で合成したBun t e塩48Fを
水160fと36チ塩酸125tの混合溶液に溶かして
90℃で8時間反応を行なったのち1反応液の一部を分
取してガスクロマド分析を行なった結果。
Reference Example 1 Bun t e salt 48F synthesized in 1) of Example 1 was dissolved in a mixed solution of 160 f of water and 125 t of 36-thihydrochloric acid and reacted at 90°C for 8 hours, after which a portion of the reaction solution was separated. The results were obtained by gas chromatography analysis.

19.3 f (反応収率73%)のβ−メルカプトプ
ロピオン酸と0.3F(反応収率1.3%)のβ−メル
カプトプロピオニトリルの生成を認めた。
The production of β-mercaptopropionic acid of 19.3 F (reaction yield 73%) and β-mercaptopropionitrile of 0.3 F (reaction yield 1.3%) was observed.

実施例2 実施例1と同様の反応器に前記製造例に示した22.9
のβ−クロロプロピオニトリル、62.71のチオ硫酸
ナトリウム5水塩および1001の水を仕込み90℃で
1時間反応させた。
Example 2 In a reactor similar to Example 1, 22.9 ml of
of β-chloropropionitrile, 62.71 parts of sodium thiosulfate pentahydrate, and 1001 parts of water were charged and reacted at 90°C for 1 hour.

次いで9滴下ロートよジ382の98チ硫酸を滴下し、
引き続き90℃で30分間反応させた。
Next, 98 thiosulfuric acid was added dropwise through the 9-dropping funnel.
Subsequently, the reaction was continued at 90°C for 30 minutes.

得うれた反応液のガスクロマトグラフ分析結果は第2表
の通シであった。
The results of gas chromatography analysis of the obtained reaction solution were as shown in Table 2.

第2表 実施例3 加水分解の反応時間を1時間にした以外は実施例2と全
く同様に反応を行なったところ、第3表に示す結果が得
られた。
Table 2 Example 3 The reaction was carried out in exactly the same manner as in Example 2 except that the hydrolysis reaction time was changed to 1 hour, and the results shown in Table 3 were obtained.

 11− 第3表 実施例4〜6 チオ硫酸塩の種類と使用量を変えた以外は実施例2と同
様に反応を行なったところ第4表に示す結果が得られた
11- Table 3 Examples 4 to 6 The reaction was carried out in the same manner as in Example 2 except that the type and amount of thiosulfate used were changed, and the results shown in Table 4 were obtained.

第4表 特許出願人 日東化学工業株式会社 代表者 難波正彦  12−Table 4 Patent applicant: Nitto Chemical Industry Co., Ltd. Representative: Masahiko Namba 12-

Claims (1)

【特許請求の範囲】[Claims] 水性媒体中でβ−クロロプロピオニトリルをチオ硫酸塩
と反応させることによシβ−メルカプトプロピオニトリ
ルの前駆体としてBunte塩を生成せしめ1次いでと
のBunte塩を酸の存在下で加水分解することを特徴
とするβ−メルカプトプロピオニトリルの製造法。
The Bunte salt is produced as a precursor to β-mercaptopropionitrile by reacting β-chloropropionitrile with thiosulfate in an aqueous medium, and the Bunte salt is then hydrolyzed in the presence of acid. A method for producing β-mercaptopropionitrile.
JP13855782A 1982-08-11 1982-08-11 Preparation of beta-mercaptopropionitrile Granted JPS5929657A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13855782A JPS5929657A (en) 1982-08-11 1982-08-11 Preparation of beta-mercaptopropionitrile

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13855782A JPS5929657A (en) 1982-08-11 1982-08-11 Preparation of beta-mercaptopropionitrile

Publications (2)

Publication Number Publication Date
JPS5929657A true JPS5929657A (en) 1984-02-16
JPS6318943B2 JPS6318943B2 (en) 1988-04-20

Family

ID=15224921

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13855782A Granted JPS5929657A (en) 1982-08-11 1982-08-11 Preparation of beta-mercaptopropionitrile

Country Status (1)

Country Link
JP (1) JPS5929657A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020095895A1 (en) * 2018-11-07 2020-05-14 株式会社資生堂 Capped container and method of manufacturing same

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5855453A (en) * 1981-09-29 1983-04-01 Kanegafuchi Chem Ind Co Ltd Preparation of optically active mercaptocarboxylic acid

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5855453A (en) * 1981-09-29 1983-04-01 Kanegafuchi Chem Ind Co Ltd Preparation of optically active mercaptocarboxylic acid

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020095895A1 (en) * 2018-11-07 2020-05-14 株式会社資生堂 Capped container and method of manufacturing same

Also Published As

Publication number Publication date
JPS6318943B2 (en) 1988-04-20

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