JPS6143157A - Production of pantethine - Google Patents
Production of pantethineInfo
- Publication number
- JPS6143157A JPS6143157A JP16446184A JP16446184A JPS6143157A JP S6143157 A JPS6143157 A JP S6143157A JP 16446184 A JP16446184 A JP 16446184A JP 16446184 A JP16446184 A JP 16446184A JP S6143157 A JPS6143157 A JP S6143157A
- Authority
- JP
- Japan
- Prior art keywords
- acid
- reaction
- pantethine
- cystamine
- organic carboxylic
- 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
Links
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、医薬品として有用なパンテチンの工業的に有
利な製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to an industrially advantageous method for producing pantethine, which is useful as a pharmaceutical.
従来の技術
従来、パンテチンの製法としては種々存在するが、工業
的にはパントテン酸とシスタミンとを縮合させる方法が
、製造工程上短く、最も経済的である。BACKGROUND OF THE INVENTION Conventionally, there are various methods for producing pantethine, but industrially, the method of condensing pantothenic acid and cystamine is the shortest and most economical method for producing pantethine.
縮合剤として、ジシクロへキシルカルボジイミド(以下
、DCCと称する)などのカルボジイミドを用いる方法
が、たとえば特公昭41−2829号公報により知られ
ているが、約30%という低収率のため、工業的実施に
あたっては必ずしも満足できるものではない。A method using carbodiimide such as dicyclohexylcarbodiimide (hereinafter referred to as DCC) as a condensing agent is known, for example, from Japanese Patent Publication No. 41-2829, but due to the low yield of about 30%, it is not suitable for industrial use. The implementation is not always satisfactory.
そこで、縮合剤としてカルボジイミドを用いて製造する
方法に際し、収率向上を目的として種々の化合物を反応
促進剤として添加する方法が提案されてきている。たと
えばDCCの存在下、反応促進剤として、ジフェニルホ
スファイト、ジエチルホスファイトなどのリン−ヒドロ
キシ化合物、またはp−トルエンスルホン酸、フエニル
スノシホン酸などのスルホン酸化合物を用いる方法(特
開昭56−133257号公報)、塩化第二鉄、塩化ア
ルミニウムなどの無機塩類を用いる方法(特開昭57−
93953号公報)、置換ヒドロキシフェノール類、ヒ
ドロキシピリミジン類、ヒドロキシキノリン類を用いる
方法(特開昭53−25520号公報)またはN−ヒド
ロキシベンゾトリアゾール、ヒドロキシスクシンイミド
を用いる方法(特開昭51−113821号公報)など
が知られている。Therefore, in the production method using carbodiimide as a condensing agent, methods have been proposed in which various compounds are added as reaction accelerators for the purpose of improving the yield. For example, a method in which a phosphorus-hydroxy compound such as diphenyl phosphite or diethyl phosphite, or a sulfonic acid compound such as p-toluenesulfonic acid or phenylsinosulfonic acid is used as a reaction accelerator in the presence of DCC (JP-A-56 -133257), a method using inorganic salts such as ferric chloride and aluminum chloride (JP-A-57-
93953), a method using substituted hydroxyphenols, hydroxypyrimidines, and hydroxyquinolines (Japanese Unexamined Patent Publication No. 53-25520), or a method using N-hydroxybenzotriazole, hydroxysuccinimide (Japanese Unexamined Patent Publication No. 113821-1982). Public bulletin) etc. are known.
発明が解決しようとする問題点
しかしながら、これらの反応促進剤は高価であったり、
あるいは反応処理が繁雑なこともあり、また目的物精製
に困難をもたらすこともあり、必ずしも工業的に有利な
製造法とは言い難い。Problems to be Solved by the Invention However, these reaction accelerators are expensive,
Alternatively, the reaction treatment may be complicated, and it may be difficult to purify the target product, so it cannot necessarily be said that it is an industrially advantageous production method.
問題点を解決するための手段
本発明者らは、これらの欠点を一掃し、工業的に有利な
パンテチンの製造方法を確立することを目的として、カ
ルボジイミドの存在下、出発原料に添加する反応促進剤
について種々検討した結果、無機酸類または有機カルボ
ン酸類が特異的に良好な促進剤となることを見出したの
である。Means for Solving the Problems In order to eliminate these drawbacks and establish an industrially advantageous method for producing pantethine, the present inventors have developed a reaction accelerator that is added to the starting materials in the presence of carbodiimide. As a result of various studies on agents, it was discovered that inorganic acids or organic carboxylic acids are specifically good accelerators.
すなわち、本発明は、パントテン酸またはその塩類とシ
スタミンまたはその塩類とをカルボジイミドの存在下縮
合させるに際し、無機酸類または有機カルボン酸類から
選ばれた少なくとも一種を反応促進剤として添加するこ
とを特徴とするパンテチンの製造方法を要旨とするもの
である。That is, the present invention is characterized in that when condensing pantothenic acid or its salts with cystamine or its salts in the presence of carbodiimide, at least one selected from inorganic acids or organic carboxylic acids is added as a reaction accelerator. The gist is a method for producing pantethine.
本発明で使用される無機酸類としては、たとえば硫酸、
塩酸、リン酸、ホウ酸などが、また有機カルボン酸類と
しては、たとえば酢酸、クロル酢酸、グリコール酸、シ
ュウ酸、サリチル酸などが挙げられる。その添加量は、
通常、原料のパントテン酸の塩に対し、0.5〜5重量
%を用いるのが好ましい。なお、本発明による上記反応
促進剤と従来の反応促進剤とを併用して用いることもで
きる。Examples of inorganic acids used in the present invention include sulfuric acid,
Examples of organic carboxylic acids include hydrochloric acid, phosphoric acid, and boric acid, and examples of organic carboxylic acids include acetic acid, chloroacetic acid, glycolic acid, oxalic acid, and salicylic acid. The amount added is
Usually, it is preferable to use 0.5 to 5% by weight based on the raw material pantothenic acid salt. Note that the reaction accelerator according to the present invention and a conventional reaction accelerator can also be used in combination.
出発原料物質は市販の入手し易いものでよく、特に塩の
形のものが好ましい。たとえば、パントテン酸の塩とし
てパントテン酸カルシウムまたはパントテン酸ナトリウ
ムが、シスタミンの塩としてシスタミン塩酸塩またはシ
スタミン硫酸塩が挙げられる。The starting materials may be commercially available materials, and those in the form of salts are particularly preferred. For example, the salt of pantothenic acid includes calcium pantothenate or sodium pantothenate, and the salt of cystamine includes cystamine hydrochloride or cystamine sulfate.
縮合剤のカルボジイミドとしては、通常、製法が容易で
、しかも安定性の点で優れ、副生ずる尿素誘導体が目的
物と分離が容易なりCCを用いるとよい。As the carbodiimide condensing agent, it is usually preferable to use CC because it is easy to produce, has excellent stability, and the by-product urea derivative can be easily separated from the target product.
溶媒としては、ピリジン、ジメチルホルムアミド、低級
アルコール、水等の単独もしくは混合溶媒を使用できる
が、好ましくは、ピリジン−水の混合溶媒がよい。As the solvent, pyridine, dimethylformamide, lower alcohol, water, etc. can be used alone or in combination, but a mixed solvent of pyridine and water is preferable.
この溶媒にパントテン酸またはその塩とシスタミンまた
はその塩、および反応促進剤として前出の無機酸類また
は有機カルボン酸類のうちの少くとも一種を溶解させ、
次いでこれにカルボジイミドを加えて縮合を行うのが便
利である。Pantothenic acid or its salt, cystamine or its salt, and at least one of the above-mentioned inorganic acids or organic carboxylic acids as a reaction promoter are dissolved in this solvent,
Conveniently, a carbodiimide is then added to carry out the condensation.
反応温度および時間については特に限定はないが、通常
、室温で5〜7時間で十分である。There are no particular limitations on the reaction temperature and time, but 5 to 7 hours at room temperature is usually sufficient.
反応終了後、目的物を常法に従って反応混合物より分離
する。たとえば、反応終了後、減圧下に溶媒を留去し、
残金に水を加え、析出する不溶物を枦取した後、炉液を
クロロホルム等の溶媒で数回洗浄する。この水溶液を酸
性イオン交換樹脂および塩基性イオン交換樹脂でそれぞ
れ処理し、濃縮することにより、分離、精製することが
できる。After the reaction is completed, the target product is separated from the reaction mixture according to a conventional method. For example, after the reaction is complete, the solvent is distilled off under reduced pressure,
After adding water to the residue and scraping off the precipitated insoluble matter, the furnace solution is washed several times with a solvent such as chloroform. Separation and purification can be achieved by treating this aqueous solution with an acidic ion exchange resin and a basic ion exchange resin, respectively, and concentrating it.
実施例
以下の実施例により本発明をより一層詳細に説明するが
、本発明はこれらに限定されるものではない。EXAMPLES The present invention will be explained in more detail with the following Examples, but the present invention is not limited thereto.
実施例1
パントテン酸カルシウム11.9g、シスタミン塩酸塩
5.6gおよび硫酸0.15 gを25%含水ピリジン
100y+j’に加え室温にて攪拌する。均一な溶液と
なった後、溶液を10℃以下に冷却し、攪拌下、DCC
I2.4gのピリジン25me溶液を注加する。注加後
、1時間冷却下で攪拌した後、室温に戻し5時間攪拌を
続ける。Example 1 11.9 g of calcium pantothenate, 5.6 g of cystamine hydrochloride and 0.15 g of sulfuric acid are added to 100y+j' of 25% hydrated pyridine and stirred at room temperature. After becoming a homogeneous solution, the solution was cooled to below 10°C, and DCC was added under stirring.
A solution of 2.4 g of I in pyridine 25me is added. After the addition, the mixture was stirred under cooling for 1 hour, then returned to room temperature and continued stirring for 5 hours.
反応終了後、浴温50℃で減圧下に濃縮する。After the reaction is completed, the mixture is concentrated under reduced pressure at a bath temperature of 50°C.
残量に水15meを加え、析出する不溶物を炉別する。Add 15 me of water to the remaining amount, and separate the precipitated insoluble matter in a furnace.
次いで25−の水で不溶物を洗浄し、洗液は炉液と合し
、50−のクロロホルムで3回洗添ス水層を150−の
アンバーライトIR−120Bを充填したカラムに通液
し、次いで流出液を150fnlのアンバーライトIR
A−410カラムに通液する。流速はそれぞれ5v=2
〜2.5で行う。Next, insoluble matter was washed with 25-ml water, and the washing liquid was combined with the furnace solution, and washed three times with 50-ml chloroform.The aqueous layer was passed through a column packed with 150-ml Amberlite IR-120B. , then the effluent was poured into 150 fnl of Amberlite IR.
Pass the solution through the A-410 column. The flow velocity is 5v=2 for each
Perform at ~2.5.
それぞれのカラムは600fneの水で洗浄し、洗浄液
は流出液と合し、50℃以下で減圧下に濃縮する。得ら
れた微黄色シロップ状のパンテチンをデシケータ−中、
五酸化リン上で減圧下に乾燥して、目的物11.5gを
得る。収率82.5%。Each column is washed with 600 fne of water, and the washings are combined with the effluent and concentrated under reduced pressure at below 50°C. The obtained slightly yellow syrupy pantethine was placed in a desiccator.
Dry over phosphorus pentoxide under reduced pressure to obtain 11.5 g of the desired product. Yield 82.5%.
実施例2
実施例1の硫酸のかわりにホウ酸0.3gとする以外は
すべて同様の操作を行い、パンテチン11.9gを得る
。収率85゜5%。Example 2 The same procedure as in Example 1 was repeated except that 0.3 g of boric acid was used instead of sulfuric acid to obtain 11.9 g of pantethine. Yield: 85.5%.
実施例3
実施例1の硫酸のかわりに塩酸0.4gとする以外はす
べて同様の操作を行い、パンテチン11.0gを得る。Example 3 The same procedure as in Example 1 was repeated except that 0.4 g of hydrochloric acid was used instead of sulfuric acid to obtain 11.0 g of pantethine.
収率79.3%。Yield 79.3%.
実施例4
実施例1の硫酸のかわりに酢酸0.6gとする以外はす
べて同様の操作を行い、パンテチン9.0gを得る。収
率65.1%。Example 4 The same procedure as in Example 1 was repeated except that 0.6 g of acetic acid was used instead of sulfuric acid to obtain 9.0 g of pantethine. Yield 65.1%.
実施例5
実施例1の硫酸のかわりにサリチル酸0.3gとする以
外はすべて同様の操作を行い、パンテチン11.2gを
得る。収率80,5%。Example 5 The same procedure as in Example 1 was repeated except that 0.3 g of salicylic acid was used instead of sulfuric acid to obtain 11.2 g of pantethine. Yield 80.5%.
かくして得られた生成物は、薄層クロマトグラフィで単
一のスポットであり、標品のパンテチンと同一のRf値
を示し、純パンテチンであることが同定された。The product thus obtained was a single spot on thin-layer chromatography, showing the same Rf value as the standard pantethine, and was identified as pure pantethine.
発明の効果
本発明のこれら反応促逸剤はごく一般品で入手し易く、
スルホン酸化合物、リン−ヒドロキシ化合物、無機塩類
またはN−ヒドロキシベンゾトリアゾールなど、従来の
ものより安価であって有利であり、また上記実施例から
明らかな通り、添加量も触媒量程度で十分な効果があり
、反応処理もし易く、目的物のパンテチンを高純度、高
収率で収得でき、製造法としては極めて工業的に有利で
ある。Effects of the Invention These reaction accelerators of the present invention are very common products and are easily available.
Sulfonic acid compounds, phosphorus-hydroxy compounds, inorganic salts, N-hydroxybenzotriazole, etc. are advantageous because they are cheaper than conventional ones, and as is clear from the above examples, sufficient effects can be achieved with the addition amount of a catalytic amount. The reaction process is easy, and the target product, pantethine, can be obtained with high purity and high yield, making it an extremely industrially advantageous manufacturing method.
Claims (1)
類とをカルボジイミドの存在下縮合させるに際し、無機
酸類または有機カルボン酸類から選ばれた少なくとも一
種を反応促進剤として添加することを特徴とするパンテ
チンの製造法。A method for producing pantethine, which comprises adding at least one selected from inorganic acids or organic carboxylic acids as a reaction accelerator when condensing pantothenic acid or its salts with cystamine or its salts in the presence of carbodiimide.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16446184A JPS6143157A (en) | 1984-08-06 | 1984-08-06 | Production of pantethine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16446184A JPS6143157A (en) | 1984-08-06 | 1984-08-06 | Production of pantethine |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62119337A Division JPS62281852A (en) | 1987-05-15 | 1987-05-15 | Production of pantethine |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6143157A true JPS6143157A (en) | 1986-03-01 |
Family
ID=15793610
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16446184A Pending JPS6143157A (en) | 1984-08-06 | 1984-08-06 | Production of pantethine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6143157A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56133257A (en) * | 1980-03-21 | 1981-10-19 | Teikoku Chem Ind Corp Ltd | Production of pantethine |
-
1984
- 1984-08-06 JP JP16446184A patent/JPS6143157A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56133257A (en) * | 1980-03-21 | 1981-10-19 | Teikoku Chem Ind Corp Ltd | Production of pantethine |
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