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JPH0261472B2 - - Google Patents
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JPH0261472B2 - - Google Patents

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Publication number
JPH0261472B2
JPH0261472B2 JP12593881A JP12593881A JPH0261472B2 JP H0261472 B2 JPH0261472 B2 JP H0261472B2 JP 12593881 A JP12593881 A JP 12593881A JP 12593881 A JP12593881 A JP 12593881A JP H0261472 B2 JPH0261472 B2 JP H0261472B2
Authority
JP
Japan
Prior art keywords
reaction
hypohalite
thiophene
alkaline
stirring
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.)
Expired
Application number
JP12593881A
Other languages
Japanese (ja)
Other versions
JPS5829783A (en
Inventor
Hiroshi Yano
Tetsuhiko Okamoto
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 Soda Co Ltd
Original Assignee
Nippon Soda 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 Nippon Soda Co Ltd filed Critical Nippon Soda Co Ltd
Priority to JP12593881A priority Critical patent/JPS5829783A/en
Publication of JPS5829783A publication Critical patent/JPS5829783A/en
Publication of JPH0261472B2 publication Critical patent/JPH0261472B2/ja
Granted legal-status Critical Current

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  • Heterocyclic Compounds Containing Sulfur Atoms (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

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

本発明は、チオフエンカルン酸類の製造方法に
係り、更に詳しくはチオフエンアルデヒド類を原
料とするチオフエンカルボン酸類の製造方法に関
するものである。 セフアロスポリン系抗生物質の中間原料等とし
て有用なチオフエンカルボン酸類は、工業的には
主としてチオフエンを出発原料としてアセチルチ
オフエンを製造し、これを酸化する方法によつて
生産されているが、この製造工程では廃棄物およ
び副生物の処理に問題が多く、また大量の酸化剤
を使用するので経済的にも不利な面が多い。チオ
フエンアルデヒド類を酸化して製造する方法とし
ては、例えば(a)フエーリング試薬による(J.A.C.
S.,75,989(1953))、(b)酸化銀による(Org.Syn.
Coll.Vol.,919),(c)ヘキサメチルリン酸トリ
アミド中で酸素を作用させる(J.O.C.30,3520
(1965))などが報告されている。しかしながらこ
れらの製造はいづれも工業的に利用し得る方法と
はいい難い。 本発明は、チオフエンアルデヒド類を、次亜ハ
ロゲン酸塩で酸化するという工業的に有利なチオ
フエンカルボン酸類の製造方法を提供するもので
ある。 すなわち、本発明は、アルカリ性水媒質中で一
般式() K0638 (式中Rは水素、ハロゲン又は低級アルキル基を
示す) で示されるチオフエンアルデヒド類を、次亜ハロ
ゲン酸塩と反応させる一般式() K0639 (式中Rは前記と同じ) の製造方法である。 本発明の方法は、水中に分散した()を次亜
ハロゲン酸塩で酸化するのであるが、()が生
成することによつて反応系が酸性になると、次亜
ハロゲン酸塩の分解がおこるから、反応系は常に
アルカリ性にしておくことが必要である。アルカ
リ性水媒質とするための水溶性アルカリ性物質と
きては、水酸化ナトリウム、水酸化カルシウムの
ようなアルカリ金属もしくはアルカリ土類金属の
水酸化物及び炭酸ナトリウムのようなアルカリ金
属炭酸塩などがあるが、実用的には水酸化ナトリ
ウムが好ましく使用される。またアルカリ性物質
の所要量は、生成する()を中和できるに充分
な量であることが必要である。従つて、例えば水
酸化ナトリウムをアルカリ性物質として使用する
場合には()と少くとも等モル使用する。また
アルカリ性物質は反応開始時から全量を添加して
も、反応の進行中に反応系の水媒質が常にアルカ
リ性になつているように適時分割して添加しても
よいが、反応開始時に全量添加しておくことが操
作上簡単である。 次亜ハロゲン酸塩としては、次亜塩素酸もしく
は次亜臭素酸のアルカリ金属塩、アルカリ土類金
属塩などがあり、次亜塩素酸ナトリウムおよび次
亜塩素酸カルシウムが実用的である。また次亜ハ
ロゲン酸塩は固型である必要はなく、水溶液とし
て使用するのであるから、工業的には有効塩素約
6〜12%の水溶液として容易に入手される次亜塩
素酸ナトリウム水溶液が好ましく使用される。次
亜ハロゲン酸塩の所要量は、その有効ハロゲン含
有量として()に対して等モル以上、好ましく
は110〜200モル%量である。 ()とアルカリ性物質とを含んだ水溶液を撹
拌下に加熱昇温してから次亜ハロゲン酸塩水溶液
を加えると、得られる()は黄色に着色するこ
とがあるから、次のように操作するのがよい。す
なわち、()とアルカリ性物質ならびに次亜ハ
ロゲン酸塩の水溶液とを混合した反応系を撹拌し
つつ除々に約50℃にまで加熱昇温し、その温度で
4〜5時間撹拌を続け、次いで約70℃に昇温して
有効ハロゲン分が消失するまで撹拌を続ける。こ
の反応により()がアルカリ塩として生成する
から、反応終了後、水と混じない有機溶媒、例え
ばトルエン、メチレンクロライドなど、で反応生
成液から未反応()を抽出除去し、水層を鉱
酸、例えば塩酸、硫酸など、でpH1〜2にして
()を析出させ、過、水洗、乾燥することに
より無色結晶の()を約80%の収率で得ること
ができる。 本発明においては、反応系の加熱を急激に行な
うと反応が激しくおこつて次亜ハロゲン酸塩の分
解が優先することがある。よつて、所要量の次亜
ハロゲン酸塩の一部を用いて反応を部分的に進め
た生成液に残部の次亜ハロゲン酸塩を加えること
によつて反応が激しく進行することを防止でき
る。 すなわち、アルカリ性水媒質中で()と
()に対して有効ハロゲンとして5〜50モル%
量の次亜ハロゲン酸塩とを50〜100℃で反応させ
た生成液に、次亜ハロゲン酸塩を50〜100℃で反
応させる。 またアルカリ性物質は、反応開始時から全量添
加しても、反応の進行中に分割添加してもよい。 反応開始時に添加する次亜ハロゲン酸塩の量
は、反応系の加熱昇温が急激に行われても反応は
激しくおこらない程度とすることが必要で、()
に対しては7〜30モル%量、好ましくは7〜30モ
ル%量、の次亜ハロゲン酸塩を添加しておく。 更に具体的に記すと、()とアルカリ性物質
ならびに上記量の次亜ハロゲン酸塩の水溶液を混
合した反応系を撹拌しつつ50〜100℃、好ましく
は約70℃、にまで加熱昇温し、同温度で2〜3時
間を費して次亜ハロゲン酸塩の残部を添加し、更
に同温度で1〜2時間撹拌を続ける。 本発明の反応系においては、水溶性の()が
反応初期には乳濁状に分散しているが、反応の進
行につれて未反応()が油滴状に集合する傾向
がある。このため反応進行中も()のアルカリ
性水媒質への分散を助けるためのテトラヒドロフ
ランのようなコソルベントあるいは界面活性剤を
反応系に加えることは、本発明を実施する上に有
益である。 以下に実施例をあげて本発明を更に説明する。
なお実施例で使用している2−チオフエンアルデ
ヒドは、チオフエンを原料とし、ウイルス−マイ
ヤー反応によつて容易の得られるものである。 実施例 1 水酸化水素原子(純度97%)4.0g(0.1モル)を
水20mlに溶解し、2−チオフエンアルデヒド
11.2g(0.1モル)と有効塩素10%の次亜塩素酸ナ
トリウム水溶液108g(0.14モル)を常温で混合し、
かきまぜながら50℃に昇温し、この温度で4時間
撹拌を続けた。次で70℃に昇温して2時間撹拌を
続けた。この時点で反応液中の有効塩素分は殆ん
ど消失した。反応生成液を冷却して、メチレンク
ロライド20mlを用いて未反応の2−チオフエンア
ルデヒドを除去し、水層に濃塩酸17mlを加えて
pH1とし、析出した結晶を取、水洗、乾燥して
無色の2−チオフエンカルボン酸(融点126〜
126.5℃)9.9gを得た。収率77.4% 実施例 2 水酸化ナトリウム(純度97%)4.0g(0.1モル)
を水20mlに溶解し、2−チオフエンアルデヒド
11.2g(0.1モル)と有効塩素10%の次亜塩素酸ナ
トリウム水溶液108g(0.14モル)のうちの11gを加
えてかきまぜながら70℃に昇温した。この温度で
撹拌を続けならがら次亜塩素酸ナトリウム水溶液
の残量を2時間を費して滴下し、さらに同温度で
1.5時間撹拌を継続した。この時点で反応後中の
有効塩素分は殆んど消失した。反応生成液を実施
例1と同様に処理して無色の2−チオフエンカル
ボン酸10.5gを得た。収率82.0%、 実施例 3〜6 実施例2とほぼ同様にして第1表に示すチオフ
エンカルボン酸類を製造した。
The present invention relates to a method for producing thiophenecarboxylic acids, and more particularly to a method for producing thiophenecarboxylic acids using thiophene aldehydes as raw materials. Thiophenecarboxylic acids, which are useful as intermediate raw materials for cephalosporin antibiotics, are produced industrially mainly by using thiophene as a starting material to produce acetylthiophene and oxidizing it. In the process, there are many problems in the treatment of waste and by-products, and since a large amount of oxidizing agent is used, there are many economic disadvantages. As a method for producing thiophenaldehydes by oxidizing them, for example, (a) Fehling's reagent (JAC
S., 75 , 989 (1953)), (b) by silver oxide (Org.Syn.
Coll.Vol., 919), (c) Oxygen in hexamethylphosphoric triamide (JOC 30 , 3520
(1965)) have been reported. However, none of these production methods can be said to be industrially applicable. The present invention provides an industrially advantageous method for producing thiophenecarboxylic acids by oxidizing thiophene aldehydes with hypohalites. That is, the present invention provides a general formula in which a thiophene aldehyde represented by the general formula () K0638 (in the formula, R represents hydrogen, halogen, or a lower alkyl group) is reacted with a hypohalite in an alkaline aqueous medium. () K0639 (in the formula, R is the same as above). In the method of the present invention, () dispersed in water is oxidized with hypohalite, but when the reaction system becomes acidic due to the formation of (), decomposition of the hypohalite occurs. Therefore, it is necessary to keep the reaction system alkaline at all times. Water-soluble alkaline substances to be used as an alkaline water medium include hydroxides of alkali metals or alkaline earth metals such as sodium hydroxide and calcium hydroxide, and alkali metal carbonates such as sodium carbonate. For practical purposes, sodium hydroxide is preferably used. Further, the amount of alkaline substance required must be sufficient to neutralize the () produced. Therefore, for example, when using sodium hydroxide as an alkaline substance, it is used in at least an equimolar amount with (). In addition, the alkaline substance may be added in its entirety from the start of the reaction, or it may be added in appropriate portions during the course of the reaction so that the aqueous medium in the reaction system is always alkaline; It is easy to operate. Examples of hypohalites include alkali metal salts and alkaline earth metal salts of hypochlorous acid or hypobromous acid, and sodium hypochlorite and calcium hypochlorite are practical. Furthermore, since the hypohalite does not need to be in solid form and is used as an aqueous solution, it is preferable to use an aqueous sodium hypochlorite solution, which is easily available industrially as an aqueous solution containing about 6 to 12% available chlorine. used. The required amount of hypohalite is at least equimolar, preferably 110 to 200 mol %, based on the effective halogen content (). If you heat an aqueous solution containing () and an alkaline substance while stirring and then add a hypohalite aqueous solution, the resulting () may turn yellow, so proceed as follows. It is better. That is, a reaction system in which () was mixed with an aqueous solution of an alkaline substance and a hypohalite was gradually heated to about 50°C while stirring, continued stirring at that temperature for 4 to 5 hours, and then heated to about 50°C. Continue stirring until the temperature rises to 70°C and the effective halogen content disappears. This reaction produces () as an alkali salt, so after the reaction is complete, unreacted () is extracted and removed from the reaction product solution using an organic solvent that does not mix with water, such as toluene or methylene chloride, and the aqueous layer is extracted with mineral acid. For example, by adjusting the pH to 1 to 2 with hydrochloric acid, sulfuric acid, etc. to precipitate (), filtering, washing with water, and drying, colorless crystals () can be obtained in a yield of about 80%. In the present invention, if the reaction system is heated rapidly, the reaction may be intense and the decomposition of the hypohalite may take priority. Therefore, by adding the remaining hypohalite to the product solution in which the reaction has partially proceeded using a portion of the required amount of hypohalite, it is possible to prevent the reaction from proceeding violently. That is, 5 to 50 mol% as effective halogen for () and () in an alkaline aqueous medium.
The product solution obtained by reacting an amount of hypohalite at 50 to 100°C is reacted with hypohalite at 50 to 100°C. Further, the alkaline substance may be added in its entirety from the start of the reaction, or may be added in portions during the progress of the reaction. The amount of hypohalite added at the start of the reaction must be such that the reaction does not occur violently even if the reaction system is heated rapidly.
Hypohalite is added in an amount of 7 to 30 mol%, preferably 7 to 30 mol%. More specifically, a reaction system in which (), an alkaline substance, and an aqueous solution of hypohalite in the above amount are mixed is heated to 50 to 100°C, preferably about 70°C, while stirring, The remainder of the hypohalite is added over 2 to 3 hours at the same temperature, and stirring is continued for an additional 1 to 2 hours at the same temperature. In the reaction system of the present invention, water-soluble (2) is dispersed in an emulsion at the initial stage of the reaction, but as the reaction progresses, unreacted (2) tends to aggregate in the form of oil droplets. For this reason, it is advantageous in carrying out the present invention to add a cosolvent or surfactant such as tetrahydrofuran to the reaction system to aid in dispersion of () in the alkaline aqueous medium during the course of the reaction. The present invention will be further explained below with reference to Examples.
The 2-thiophene aldehyde used in the examples is made from thiophene and can be easily obtained by the Wills-Meyer reaction. Example 1 4.0 g (0.1 mol) of hydrogen hydroxide atoms (purity 97%) was dissolved in 20 ml of water, and 2-thiophenaldehyde
Mix 11.2g (0.1mol) and 108g (0.14mol) of an aqueous sodium hypochlorite solution with 10% available chlorine at room temperature.
The temperature was raised to 50°C while stirring, and stirring was continued at this temperature for 4 hours. Next, the temperature was raised to 70°C and stirring was continued for 2 hours. At this point, most of the available chlorine in the reaction solution disappeared. The reaction product solution was cooled, unreacted 2-thiophenaldehyde was removed using 20 ml of methylene chloride, and 17 ml of concentrated hydrochloric acid was added to the aqueous layer.
The pH was adjusted to 1, the precipitated crystals were collected, washed with water, and dried to produce colorless 2-thiophenecarboxylic acid (melting point 126~
126.5°C) 9.9g was obtained. Yield 77.4% Example 2 Sodium hydroxide (purity 97%) 4.0g (0.1 mol)
Dissolve 2-thiophenaldehyde in 20ml of water.
11.2 g (0.1 mol) and 11 g of 108 g (0.14 mol) of an aqueous sodium hypochlorite solution containing 10% available chlorine were added, and the temperature was raised to 70°C while stirring. While continuing to stir at this temperature, the remaining amount of the sodium hypochlorite aqueous solution was added dropwise over 2 hours, and then at the same temperature.
Stirring was continued for 1.5 hours. At this point, most of the available chlorine content after the reaction had disappeared. The reaction product solution was treated in the same manner as in Example 1 to obtain 10.5 g of colorless 2-thiophenecarboxylic acid. Yield: 82.0%. Examples 3 to 6 The thiophenecarboxylic acids shown in Table 1 were produced in substantially the same manner as in Example 2.

【表】 実施例 7 実施例2における70℃での次亜塩素酸ナトリウ
ム水溶液の滴下をはじめる前に反応液中にロート
油5mlを加えた他は実施例2と同様に反応を行
い、反応終了後、メチレンクロライドでの未反応
の2−チオフエンアルデヒド除去を行わずに塩酸
で酸析し、析出物を水洗、乾燥して2−チオフエ
ンカルボン酸11.1gを得た。収率87.0%。
[Table] Example 7 The reaction was carried out in the same manner as in Example 2, except that 5 ml of funnel oil was added to the reaction solution before starting the dropwise addition of the sodium hypochlorite aqueous solution at 70°C in Example 2, and the reaction was completed. Thereafter, without removing unreacted 2-thiophene aldehyde with methylene chloride, acid precipitation was performed with hydrochloric acid, and the precipitate was washed with water and dried to obtain 11.1 g of 2-thiophenecarboxylic acid. Yield 87.0%.

Claims (1)

【特許請求の範囲】 1 アルカリ性水媒質中にて、一般式 K0636 (式中Rは水素、ハロゲン又は低級アルキル基を
あらわす) で示されるチオフエンアルデヒド類を、次亜ハロ
ゲン酸塩と反応させることを特徴とする一般式 K0637 (式中Rは前記と同じ) で示されるチオフエンカルボン酸塩の製造方法。 2 チオフエンアルデヒド類と、該アルデヒド類
に対して有効ハロゲンとして5〜50モル%量の次
亜ハロゲン酸塩とを50〜100℃で反応させた生成
液に、次亜ハロゲン酸塩を50〜100℃で反応させ
る特許請求の範囲第1項記載の製造方法。
[Claims] 1. Reacting a thiophene aldehyde represented by the general formula K0636 (wherein R represents hydrogen, halogen, or a lower alkyl group) with a hypohalite in an alkaline aqueous medium. A method for producing a thiophene carboxylate represented by the general formula K0637 (wherein R is the same as above), characterized by: 2. Add 50 to 50% of hypohalite to the product solution obtained by reacting thiophene aldehydes and hypohalite in an amount of 5 to 50 mol% as an effective halogen to the aldehydes at 50 to 100°C. The manufacturing method according to claim 1, wherein the reaction is carried out at 100°C.
JP12593881A 1981-08-13 1981-08-13 Preparation of thiophenecarboxylic acid Granted JPS5829783A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12593881A JPS5829783A (en) 1981-08-13 1981-08-13 Preparation of thiophenecarboxylic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12593881A JPS5829783A (en) 1981-08-13 1981-08-13 Preparation of thiophenecarboxylic acid

Publications (2)

Publication Number Publication Date
JPS5829783A JPS5829783A (en) 1983-02-22
JPH0261472B2 true JPH0261472B2 (en) 1990-12-20

Family

ID=14922675

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12593881A Granted JPS5829783A (en) 1981-08-13 1981-08-13 Preparation of thiophenecarboxylic acid

Country Status (1)

Country Link
JP (1) JPS5829783A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63140089A (en) * 1986-12-01 1988-06-11 Anelva Corp Method and device for etching aluminum alloy film
CN101906092B (en) * 2009-06-04 2013-07-03 浙江医药股份有限公司新昌制药厂 Preparation method of 2-thiophenecarboxylic acid
CN103232430A (en) * 2013-04-30 2013-08-07 威海迪素制药有限公司 Preparation method of rivaroxaban intermediate 5-chlorothiophene-2-carboxylic acid
CN118496197A (en) * 2019-12-20 2024-08-16 拜耳公司 Substituted thiophenecarboxamides, thiophenecarboxylic acids and derivatives thereof

Also Published As

Publication number Publication date
JPS5829783A (en) 1983-02-22

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