JPH06345723A - Production of mercaptobenzamide - Google Patents

Production of mercaptobenzamide

Info

Publication number
JPH06345723A
JPH06345723A JP16603093A JP16603093A JPH06345723A JP H06345723 A JPH06345723 A JP H06345723A JP 16603093 A JP16603093 A JP 16603093A JP 16603093 A JP16603093 A JP 16603093A JP H06345723 A JPH06345723 A JP H06345723A
Authority
JP
Japan
Prior art keywords
mercaptobenzamide
sulfide
halogenobenzamide
polar solvent
reaction
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
JP16603093A
Other languages
Japanese (ja)
Inventor
Koji Shimada
康次 島田
Hiroshi Itsuda
博 五田
Kaoru Nagaoka
薫 長岡
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.)
Sumitomo Seika Chemicals Co Ltd
Original Assignee
Sumitomo Seika Chemicals 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 Sumitomo Seika Chemicals Co Ltd filed Critical Sumitomo Seika Chemicals Co Ltd
Priority to JP16603093A priority Critical patent/JPH06345723A/en
Publication of JPH06345723A publication Critical patent/JPH06345723A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To simply obtain mercaptobenzamide useful as an intermediate for medicines, agrichemicals, etc., in good yield without using a heavy metal by reacting an o- or a p-halogenobenzamide with a sulfide in a polar solvent. CONSTITUTION:An o- or a p-halogenobenzamide expressed by formula 1 (X is Cl or Br) reacts with a sulfide in a polar solvent (an alkylamide such as N-methyl-2-pyrrolidone is especially preferred) to afford o- or p- mercaptobenzmide expressed by formula 2. Since a reducing step is absent and a heavy metal is not used, the method for production is industrially advantageous without any problems in environmental pollution due to waste liquors thereof. The mercaptobenzamide is useful as a raw material for thiosalicylic acid which is a raw material for thioindigo coloring matters.

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、農薬等の中間体
として有用な化合物であるメルカプトベンズアミドの製
造法に関する。メルカプトベンズアミドはチオインジゴ
色素の原料であるチオサリチル酸の原料としても有用で
ある。
FIELD OF THE INVENTION The present invention relates to a process for producing mercaptobenzamide which is a compound useful as an intermediate for medicines, agricultural chemicals and the like. Mercaptobenzamide is also useful as a raw material for thiosalicylic acid, which is a raw material for thioindigo dyes.

【0002】[0002]

【従来の技術】従来、メルカプトベンズアミドの製造方
法としては、 チオサリチル酸を塩化第二鉄および濃塩酸とともに
加熱反応せしめてジチオサリチル酸となし、次いでこれ
をハロゲン化してジチオサリチル酸ハロゲニドを得、更
にこれをアンモニアと反応させて2,2’−ジチオビス
ベンズアミドとし、これを鉱酸中、亜鉛により還元する
方法(特開昭52−108983号公報)、及び クロロベンズアミドをジメチルスルホキシド(DM
SO)及びN,N−ジメチルホルムアミド(DMF)溶
媒中、水硫化ソーダと反応させ、2,2’−ジチオビス
ベンズアミドとなし、これを鉱酸中、亜鉛により還元す
る方法(特開昭51−131847号公報)等が知られ
ている。
Conventionally, as a method for producing mercaptobenzamide, thiosalicylic acid is heated and reacted with ferric chloride and concentrated hydrochloric acid to form dithiosalicylic acid, which is then halogenated to obtain dithiosalicylic acid halogenide. A method of reacting with ammonia to form 2,2'-dithiobisbenzamide, which is reduced with zinc in mineral acid (JP-A-52-108983), and chlorobenzamide is converted into dimethyl sulfoxide (DM).
SO) and N, N-dimethylformamide (DMF) in a solvent to react with sodium hydrosulfide to give 2,2′-dithiobisbenzamide, which is reduced with zinc in a mineral acid (JP-A-51- No. 131847) is known.

【0003】[0003]

【発明が解決しようとする課題】上記した、従来公知の
製造方法は、いずれも一旦ジスルフィドを生成させた
後、還元によりメルカプトベンズアミドを得るため、工
程が煩雑であるばかりでなく、還元に際しては、人体に
有害な亜鉛等の重金属を使用するため、その廃液による
環境汚染が大きな問題となるなど種々の欠点を含んでお
り、工業的に優れた方法であるとは言い難い。本発明は
このような課題を解決するものであり、その目的は重金
属を使用することなく、簡便にメルカプトベンズアミド
を製造する方法を提供することにある。
In all of the above-mentioned conventionally known production methods, since mercaptobenzamide is obtained by reduction after once producing disulfide, not only the steps are complicated, but also in the case of reduction, Since heavy metals such as zinc, which are harmful to the human body, are used, there are various drawbacks such as environmental pollution caused by the waste liquid, which is a serious problem, and it cannot be said that the method is industrially excellent. The present invention solves such a problem, and an object thereof is to provide a method for easily producing mercaptobenzamide without using a heavy metal.

【0004】[0004]

【課題を解決するための手段】本発明者らは、上記した
状況に鑑み、簡便かつ工業的に有利にメルカプトベンズ
アミドを製造する方法を提供すべく鋭意検討した。その
結果、ハロゲノベンズアミドを極性溶媒中、硫化物によ
りチオール化することで、目的とするメルカプトベンズ
アミドが得られることを見いだし本発明に至った。本発
明において、副反応物として得られるジスルフィド化合
物の生成が少量であることは特異なことであった。
In view of the above-mentioned situation, the present inventors have earnestly studied to provide a method for producing mercaptobenzamide conveniently and industrially advantageously. As a result, they have found that the desired mercaptobenzamide can be obtained by thiolating a halogenobenzamide with a sulfide in a polar solvent, and completed the present invention. In the present invention, it was peculiar that the disulfide compound obtained as a side reaction product was produced in a small amount.

【0005】[0005]

【化2】 [Chemical 2]

【0006】すなわち本発明の要旨は、一般式(1)で
表されるオルトまたはパラハロゲノベンズアミドを極性
溶媒中、硫化物と反応させることを特徴とする、オルト
またはパラメルカプトベンズアミドの製造法である。
That is, the gist of the present invention is a process for producing ortho or paramercaptobenzamide, which comprises reacting ortho or parahalogenobenzamide represented by the general formula (1) with a sulfide in a polar solvent. .

【0007】[0007]

【化3】 (但し、Xは塩素原子又は臭素原子を表わす。)[Chemical 3] (However, X represents a chlorine atom or a bromine atom.)

【0008】本発明によるメルカプトベンズアミドの製
造方法は、工程が短く、また高収率で目的物が得られる
ため工業的にも有利な方法と言える。さらに従来の方法
において還元反応に用いる重金属は、全く使用しないた
め廃液による環境汚染等の問題もない。以下に本発明を
詳細に説明する。
The method for producing mercaptobenzamide according to the present invention is industrially advantageous because the steps are short and the desired product can be obtained in high yield. Furthermore, since the heavy metal used in the reduction reaction in the conventional method is not used at all, there is no problem of environmental pollution due to waste liquid. The present invention will be described in detail below.

【0009】本発明において使用する原料のハロゲノベ
ンズアミドとしては、オルトまたはパラハロゲノベンズ
アミドが用いられ、その具体例としては、o−クロロベ
ンズアミド、p−クロロベンズアミド、o−ブロムベン
ズアミド、p−ブロムベンズアミド等が挙げられる。前
記ハロゲノベンズアミドは公知の方法、例えばハロゲノ
安息香酸を塩化チオニル等の塩素化剤により塩素化し、
アンモニアによりアミド化することにより容易に得るこ
とができる。
The starting halogenobenzamide used in the present invention is ortho or para-halogenobenzamide, and specific examples thereof include o-chlorobenzamide, p-chlorobenzamide, o-bromobenzamide, p-bromobenzamide and the like. Is mentioned. The halogenobenzamide is a known method, for example, chlorination of halogenobenzoic acid with a chlorinating agent such as thionyl chloride,
It can be easily obtained by amidation with ammonia.

【0010】本発明においてチオール化剤として用いる
硫化物としては、通常、硫化アルカリが用いられ、特
に、硫化ソーダ、水硫化ソーダあるいは、その水和物が
好ましく用いられる。その使用量は、ハロゲノベンズア
ミド1モルに対し、1.0〜10倍モルの範囲であり、
好ましくは1〜3倍モルの範囲である。使用量が1.0
倍モル未満では未反応のハロゲノベンズアミドが増加
し、収量が少なくなり、一方、10倍モルを越えて使用
してもそれに見合う効果が得られないので、得策ではな
い。
As the sulfide used as the thiolating agent in the present invention, alkali sulfide is usually used, and sodium sulfide, sodium hydrosulfide or a hydrate thereof is particularly preferably used. The amount used is in the range of 1.0 to 10 times by mole with respect to 1 mol of halogenobenzamide,
It is preferably in the range of 1 to 3 times by mole. Usage is 1.0
If the amount is less than twice the molar amount, the amount of unreacted halogenobenzamide increases and the yield decreases. On the other hand, if the amount exceeds 10 times the molar amount, the corresponding effect cannot be obtained.

【0011】本発明においては、前記したハロゲノベン
ズアミドと硫化物の反応を極性溶媒中で行うことを特徴
とする。使用する極性溶媒としては、アルキルアミドが
用いられ、通常C1 〜C4 のアルキル基を持つアルキル
アミド、例えばN−メチル−2−ピロリドン(以下、N
MPと略す)、ジメチルホルムアミド(以下、DMFと
略す)、ジメチルアセトアミド等が挙げられ、なかでも
NMPを用いると好結果が得られる。溶媒の使用量は、
ハロゲノベンズアミド1重量部に対し通常2〜20重量
部、好ましくは5〜10重量部が使用される。溶媒の使
用量が2重量部より少ないと硫化物の溶解が不充分とな
り収率が低下し、20重量部を越えて用いた場合は、容
積効率の点で不利となる。
The present invention is characterized in that the above-mentioned reaction of halogenobenzamide and sulfide is carried out in a polar solvent. The polar solvent used is an alkylamide, which is usually an alkylamide having a C 1 to C 4 alkyl group, such as N-methyl-2-pyrrolidone (hereinafter, referred to as N-methyl-2-pyrrolidone).
Examples thereof include MP), dimethylformamide (hereinafter abbreviated as DMF), dimethylacetamide, and the like. Among them, good results are obtained by using NMP. The amount of solvent used is
Usually, 2 to 20 parts by weight, preferably 5 to 10 parts by weight, is used with respect to 1 part by weight of halogenobenzamide. If the amount of the solvent used is less than 2 parts by weight, dissolution of the sulfide will be insufficient and the yield will decrease, and if used in excess of 20 parts by weight, it will be disadvantageous in terms of volumetric efficiency.

【0012】反応温度は通常80〜200℃の範囲、好
ましくは120〜180℃の範囲である。反応温度が8
0℃未満では、反応速度が遅くなり、200℃を越える
と副反応が起こるため目的物の収率が低下する。反応の
進行は、高速液体クロマトグラフィー等の適当な分析手
段により原料物質の減少および生成物の増加等で確認す
ることができる。反応時間は、反応温度、原料仕込みモ
ル比等の反応条件にもよるが、通常、1〜15時間で反
応は完結する。反応終了後、溶媒を留去したのち、水を
添加し塩酸等の鉱酸により系を酸性化することにより生
成物が酸析され、これを濾過することで目的物であるメ
ルカプトベンズアミドを取得することができる。
The reaction temperature is usually in the range of 80 to 200 ° C, preferably 120 to 180 ° C. Reaction temperature is 8
If the temperature is lower than 0 ° C, the reaction rate becomes slow, and if the temperature exceeds 200 ° C, a side reaction occurs, so that the yield of the target substance decreases. The progress of the reaction can be confirmed by a decrease in the raw material and an increase in the product by an appropriate analytical means such as high performance liquid chromatography. The reaction time depends on the reaction conditions such as the reaction temperature and the molar ratio of the raw materials charged, but the reaction is usually completed in 1 to 15 hours. After completion of the reaction, the solvent is distilled off, water is added, and the product is acidified by acidifying the system with a mineral acid such as hydrochloric acid, and the product is filtered to obtain the desired product, mercaptobenzamide. be able to.

【0013】[0013]

【実施例】以下、実施例により本発明をさらに詳しく説
明するが、本発明はこれらの実施例によりなんら限定さ
れるものではない。
The present invention will be described in more detail with reference to the following examples, but the present invention is not limited to these examples.

【0014】実施例1 撹拌機、温度計、冷却器を備えた200ml3つ口フラ
スコに、o−クロロベンズアミド15.6g(0.10
mol)、60%硫化ソーダ16.0g(0.12mo
l)及びNMP100gを仕込み、160℃で4時間撹
拌した。反応後減圧下でNMPを留去した後、水100
gで希釈し、濃塩酸を添加し、系内を酸性化した。析出
した結晶を濾取し、乾燥することによりo−メルカプト
ベンズアミド13.0gを得た。原料o−クロロベンズ
アミドに対する収率は85%であった。
EXAMPLE 1 15.6 g (0.10 g) of o-chlorobenzamide was placed in a 200 ml three-necked flask equipped with a stirrer, a thermometer and a condenser.
mol), 60% sodium sulfide 16.0 g (0.12 mo)
1) and 100 g of NMP were charged, and the mixture was stirred at 160 ° C. for 4 hours. After the reaction, NMP was distilled off under reduced pressure, and then water 100 was added.
The mixture was diluted with g and concentrated hydrochloric acid was added to acidify the system. The precipitated crystals were collected by filtration and dried to obtain 13.0 g of o-mercaptobenzamide. The yield based on the raw material o-chlorobenzamide was 85%.

【0015】実施例2 o−クロロベンズアミドに代えてo−ブロモベンズアミ
ド20.0g(0.10mol)を用いる以外は、実施
例1と同様にして反応を行った。o−メルカプトベンズ
アミドの収量は、13.7gであり、o−ブロモベンズ
アミドに対する収率は90%であった。
Example 2 The reaction was carried out in the same manner as in Example 1 except that 20.0 g (0.10 mol) of o-bromobenzamide was used instead of o-chlorobenzamide. The yield of o-mercaptobenzamide was 13.7 g, and the yield based on o-bromobenzamide was 90%.

【0016】実施例3 o−クロロベンズアミドに代えてo−ブロモベンズアミ
ド20.0g(0.10mol)を、60%硫化ソーダ
に代えて70%水硫化ソーダ9.6g(0.12mo
l)を用いる以外は、実施例1と同様にして反応を行っ
た。o−メルカプトベンズアミドの収量は、12.3g
であり、o−ブロモベンズアミドに対する収率は81%
であった。
Example 3 20.0 g (0.10 mol) of o-bromobenzamide was used instead of o-chlorobenzamide, and 9.6 g of 70% sodium hydrosulfide was used instead of 60% sodium sulfide.
The reaction was performed in the same manner as in Example 1 except that 1) was used. The yield of o-mercaptobenzamide was 12.3 g.
And the yield based on o-bromobenzamide is 81%.
Met.

【0017】実施例4 o−クロロベンズアミドに代えてp−クロロベンズアミ
ド15.5g(0.10mol)を用いる以外は、実施
例1と同様にして反応を行った。p−メルカプトベンズ
アミドの収量は、11.4gであり、p−クロロベンズ
アミドに対する収率は75%であった。
Example 4 The reaction was carried out in the same manner as in Example 1 except that 15.5 g (0.10 mol) of p-chlorobenzamide was used instead of o-chlorobenzamide. The yield of p-mercaptobenzamide was 11.4 g, and the yield based on p-chlorobenzamide was 75%.

【0018】実施例5 溶媒をNMPに代えてDMF100gを用い、反応条件
を130℃で7時間とする以外は、実施例1と同様にし
て反応を行った。o−メルカプトベンズアミドの収量
は、10.5gであり、o−クロロベンズアミドに対す
る収率は69%であった。
Example 5 A reaction was carried out in the same manner as in Example 1 except that 100 g of DMF was used instead of NMP as the solvent and the reaction conditions were 130 ° C. and 7 hours. The yield of o-mercaptobenzamide was 10.5 g, and the yield based on o-chlorobenzamide was 69%.

【0019】[0019]

【発明の効果】本発明によれば、オルトまたはパラハロ
ゲノベンズアミドを極性溶媒中、硫化物と反応させると
いう簡便な方法により、収率よく目的とするオルトまた
はパラメルカプトベンズアミドを製造することができ
る。従来公知の方法のように還元工程がなく、重金属を
使用することがないため、その廃液による環境汚染問題
もなく工業的に有利にメルカプトベンズアミドを製造す
ることができる。
INDUSTRIAL APPLICABILITY According to the present invention, the desired ortho or paramercaptobenzamide can be produced in good yield by a simple method of reacting ortho or parahalogenobenzamide with a sulfide in a polar solvent. Unlike the conventionally known method, there is no reduction step and no heavy metal is used. Therefore, mercaptobenzamide can be industrially produced without any problem of environmental pollution due to the waste liquid.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 一般式(1)で表されるオルトまたはパ
ラハロゲノベンズアミドを極性溶媒中、硫化物と反応さ
せることを特徴とする、オルトまたはパラメルカプトベ
ンズアミドの製造法。 【化1】 (但し、Xは塩素原子又は臭素原子を表わす。)
1. A method for producing ortho or paramercaptobenzamide, which comprises reacting ortho or parahalogenobenzamide represented by the general formula (1) with a sulfide in a polar solvent. [Chemical 1] (However, X represents a chlorine atom or a bromine atom.)
【請求項2】 極性溶媒がアルキルアミドである請求項
1記載の製造法。
2. The method according to claim 1, wherein the polar solvent is an alkylamide.
【請求項3】 アルキルアミドがN−メチル−2−ピロ
リドンであることを特徴とする請求項2記載の製造法。
3. The method according to claim 2, wherein the alkylamide is N-methyl-2-pyrrolidone.
JP16603093A 1993-06-10 1993-06-10 Production of mercaptobenzamide Pending JPH06345723A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16603093A JPH06345723A (en) 1993-06-10 1993-06-10 Production of mercaptobenzamide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16603093A JPH06345723A (en) 1993-06-10 1993-06-10 Production of mercaptobenzamide

Publications (1)

Publication Number Publication Date
JPH06345723A true JPH06345723A (en) 1994-12-20

Family

ID=15823648

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16603093A Pending JPH06345723A (en) 1993-06-10 1993-06-10 Production of mercaptobenzamide

Country Status (1)

Country Link
JP (1) JPH06345723A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8143447B2 (en) * 2006-09-05 2012-03-27 Bipar Sciences, Inc. Treatment of cancer
WO2013060766A1 (en) 2011-10-26 2013-05-02 Titan Chemicals Limited Process for preparing 1,2-benzisothiazolin-3-one
WO2014173716A1 (en) 2013-04-23 2014-10-30 Titan Chemicals Limited Process for preparing 1,2-benzisothiazolin-3-ones

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8143447B2 (en) * 2006-09-05 2012-03-27 Bipar Sciences, Inc. Treatment of cancer
WO2013060766A1 (en) 2011-10-26 2013-05-02 Titan Chemicals Limited Process for preparing 1,2-benzisothiazolin-3-one
US8476452B2 (en) 2011-10-26 2013-07-02 Titan Chemicals Limited Process for preparing 1,2-benzoisothiazoline-3-one
JP2015501312A (en) * 2011-10-26 2015-01-15 チタン ケミカルズ リミテッドTitan Chemicals Limited Method for synthesizing 1,2-benzisothiazolin-3-one
RU2614424C2 (en) * 2011-10-26 2017-03-28 Титан Кемикалс Лимитед Method of producing 1,2-benzisothiazolin-3-one
WO2014173716A1 (en) 2013-04-23 2014-10-30 Titan Chemicals Limited Process for preparing 1,2-benzisothiazolin-3-ones
US9067899B2 (en) 2013-04-23 2015-06-30 Titan Chemicals Limited Process for preparing 1,2-benzoisothiazolin-3-ones
CN105283447A (en) * 2013-04-23 2016-01-27 泰坦化工有限公司 Process for preparing 1,2-benzisothiazolin-3-ones

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