JP3229658B2 - Method for producing N-acetyl-DL-tryptophan - Google Patents

Method for producing N-acetyl-DL-tryptophan

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Publication number
JP3229658B2
JP3229658B2 JP21016192A JP21016192A JP3229658B2 JP 3229658 B2 JP3229658 B2 JP 3229658B2 JP 21016192 A JP21016192 A JP 21016192A JP 21016192 A JP21016192 A JP 21016192A JP 3229658 B2 JP3229658 B2 JP 3229658B2
Authority
JP
Japan
Prior art keywords
tryptophan
acetic anhydride
acetyl
aqueous solution
acetylation
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 - Fee Related
Application number
JP21016192A
Other languages
Japanese (ja)
Other versions
JPH0656775A (en
Inventor
長原  清輝
隆一 三田
信裕 福原
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.)
Mitsui Chemicals Inc
Original Assignee
Mitsui Chemicals Inc
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 Mitsui Chemicals Inc filed Critical Mitsui Chemicals Inc
Priority to JP21016192A priority Critical patent/JP3229658B2/en
Publication of JPH0656775A publication Critical patent/JPH0656775A/en
Application granted granted Critical
Publication of JP3229658B2 publication Critical patent/JP3229658B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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、アルカリ金属水酸化物
の水溶液中でL−トリプトファンと無水酢酸からN−ア
セチル−DL−トリプトファンを得る改善された製造方
法に関する。
The present invention relates to an improved process for obtaining N-acetyl-DL-tryptophan from L-tryptophan and acetic anhydride in an aqueous solution of an alkali metal hydroxide.

【0002】[0002]

【従来の技術】L−トリプトファンをアルカリ金属水酸
化物の水溶液中で無水酢酸を用いるN−アセチル−DL
−トリプトファンの製造方法〔ザ・ジャーナル・オブ・
バイオロジカル・ケミストリー Vol.XCVI N
o.2 P511〜517(The Journal
of Biological Chemistry)〕
は知られている。該方法はL−トリプトファンに対して
約2倍モルの苛性ソーダ水溶液にL−トリプトファンを
溶解し、L−トリプトファンに対し約6倍モルの無水酢
酸を数回に分けて、激しく攪拌しながら加える。その
後、溶液の温度を35〜40℃に3時間保持すると結晶
が析出してくるので、混合物を冷却し、結晶を分離、水
洗等の後処理を行い目的物を得ている。しかし該方法で
の収率はたかだか75%と低く改良が望まれていた。
2. Description of the Related Art N-acetyl-DL using acetic anhydride in an aqueous solution of an alkali metal hydroxide is used for L-tryptophan.
-Method for producing tryptophan [The Journal of
Biological Chemistry Vol. XCVI N
o. 2 P511-517 (The Journal
of Biological Chemistry)]
Is known. In this method, L-tryptophan is dissolved in an aqueous caustic soda solution having a molar ratio of about 2 times L-tryptophan, and acetic anhydride having a molar ratio of about 6 times L-tryptophan is added in several portions with vigorous stirring. Thereafter, when the temperature of the solution is maintained at 35 to 40 ° C. for 3 hours, crystals precipitate. Therefore, the mixture is cooled, the crystals are separated, and post-treatments such as washing with water are performed to obtain the desired product. However, the yield by this method was as low as 75% at most, and improvement was desired.

【0003】[0003]

【発明が解決しようとする課題】本発明は従来方法の収
率が低いと言う欠点を克服し、簡単な操作でしかも工業
的に有利に実施することが出来るN−アセチル−DL−
トリプトファンの製造方法を提供することにある。
SUMMARY OF THE INVENTION The present invention overcomes the drawbacks of the conventional method in that the yield is low, and can be carried out with simple operation and industrially advantageously.
An object of the present invention is to provide a method for producing tryptophan.

【0004】[0004]

【課題を解決するための手段】本発明者らは前記課題を
解決する為鋭意研究を重ねた結果、アセチル化時のpH
を11以上に管理し、ラセミ化時の反応液を均一状態で
行う事により、高品質、高収率でN−アセチル−DL−
トリプトファンを製造できる事を見い出し、本発明を完
成するに至った。
Means for Solving the Problems The inventors of the present invention have conducted intensive studies to solve the above-mentioned problems, and as a result, the pH at the time of acetylation has been improved.
Is controlled to 11 or more, and the reaction solution at the time of racemization is performed in a uniform state, so that N-acetyl-DL-
They have found that tryptophan can be produced, and have completed the present invention.

【0005】即ち、本発明はL−トリプトファンをアル
カリ水溶液中で無水酢酸と反応させN−アセチル−DL
−トリプトファンを製造する方法に於いて、L−トリプ
トファン及びL−トリプトファンに対しモル量のアル
カリ金属水酸化物の水溶液に、該水溶液のpHを11以
上に保ちながら、無水酢酸とアルカリ金属水酸化物水溶
液を同時に加えてアセチル化を行い、引き続き水溶液を
加熱下、無水酢酸で処理する事を特徴とするN−アセチ
ル−DL−トリプトファンの製造方法である。本発明の
方法で用いられるL−トリプトファンは合成法、酵素
法、発酵法のいずれの方法で製造されたものでも使用出
来る。
That is, the present invention relates to the reaction of N-acetyl-DL by reacting L-tryptophan with acetic anhydride in an aqueous alkaline solution.
In a method for producing tryptophan, acetic anhydride and alkali metal hydroxide are added to an aqueous solution of L-tryptophan and an alkali metal hydroxide in an equimolar amount to L-tryptophan while maintaining the pH of the aqueous solution at 11 or more. A method for producing N-acetyl-DL-tryptophan, characterized by simultaneously adding an aqueous solution of the compound and performing acetylation, and subsequently treating the aqueous solution with acetic anhydride while heating. The L-tryptophan used in the method of the present invention may be one produced by any of a synthetic method, an enzymatic method and a fermentation method.

【0006】本発明の方法で用いられるアルカリ金属水
酸化物は、例えば水酸化カリウム、水酸化ナトリウム等
が挙げられ、L−トリプトファン水溶液の調整に対し
モル量が使用される。等モル未満では不純物が副生し、
かつラセミ化率が低下する。等モル量を越えて用いると
ラセミ化後、N−アセチル−DL−トリプトファンの析
出の為に多量の鉱酸が必要となり、品質、収率の低下を
招く原因となり好ましくない。
[0006] alkali metal hydroxide used in the method of the present invention, for example potassium hydroxide, sodium hydroxide and the like, etc. <br/> molar amount with respect to adjustment of L- tryptophan solution is used. If less than equimolar, impurities are by-produced,
And the racemization rate decreases. If used in an equimolar amount, after racemization, a large amount of mineral acid is required for the precipitation of N-acetyl-DL-tryptophan, which is unfavorable because it causes a decrease in quality and yield.

【0007】本発明の方法では先ず、第一段としてアセ
チル化反応を行い、次にラセミ化を実施し目的物を得
る。アセチル化の条件はL−トリプトファンのアルカリ
金属水酸化物の水溶液に無水酢酸を間欠的または連続的
に添加しながら行う。一時に無水酢酸を添加するとアセ
チル化収率が低下するので好ましくない。更にアセチル
化時の無水酢酸の使用量はL−トリプトファンに対し1
〜2倍モル、好ましくは1倍モルである。無水酢酸を添
加する時の反応液のpHは11以上、好ましくはpH1
1〜13の範囲に保ちながら実施する。反応液のpHが
11未満であれば不純物が副生し純度が低下する。
In the method of the present invention, first, an acetylation reaction is carried out as a first step, and then a racemization is carried out to obtain an intended product. The acetylation is performed while intermittently or continuously adding acetic anhydride to an aqueous solution of an alkali metal hydroxide of L-tryptophan. It is not preferable to add acetic anhydride at one time because the yield of acetylation decreases. Further, the amount of acetic anhydride used for acetylation is 1 to L-tryptophan.
22 moles, preferably 1 mole. When acetic anhydride is added, the pH of the reaction solution is 11 or more, preferably pH 1
It is carried out while maintaining the range of 1 to 13. If the pH of the reaction solution is less than 11, impurities are produced as by-products and the purity is reduced.

【0008】アセチル化時の反応液のpHを11以上に
管理するにはpHコントローラあるいは反応液のpHを
pHメーター等で常に測定し、pHが11以上を保持す
るようにアルカリ金属水酸化物の水溶液を加えることで
達成される。アセチル化時の反応温度は0〜50℃、好
ましくは20〜40℃であり、アセチル化時の無水酢酸
の添加時間は1〜5時間、好ましくは2〜3時間、アセ
チル化熟成時間は1〜2時間で十分である。
In order to control the pH of the reaction solution at the time of acetylation to 11 or more, the pH of the reaction solution is constantly measured with a pH controller or a pH meter, and the pH of the alkali metal hydroxide is kept at 11 or more. This is achieved by adding an aqueous solution. The reaction temperature at the time of acetylation is 0 to 50 ° C., preferably 20 to 40 ° C., the addition time of acetic anhydride at the time of acetylation is 1 to 5 hours, preferably 2 to 3 hours, and the acetylation ripening time is 1 to 5 hours. Two hours is enough.

【0009】アセチル化が終了したら引き続きラセミ化
を行う。ラセミ化はアセチル化反応液を60〜100
℃、好ましくは70〜80℃に昇温し、反応液中に析出
している結晶を溶解し、均一状態にしてその温度におい
て無水酢酸をL−トリプトファンに対し2〜5倍モル、
好ましくは3〜4倍モル添加して実施する。ラセミ化時
の無水酢酸の添加時間は1〜4時間、好ましくは2〜3
時間である。ラセミ化反応熟成後、反応液を冷却、酸
析、結晶を分離し、水洗等の常法の後処理を行い目的物
を得る事が出来る。
When the acetylation is completed, the racemization is subsequently performed. For racemization, the acetylation reaction solution is 60-100
C., preferably 70-80 ° C., dissolving the crystals precipitated in the reaction solution to make it uniform, and at that temperature, add acetic anhydride at a temperature 2-5 times mol of L-tryptophan;
It is preferably carried out by adding 3 to 4 times mol. The addition time of acetic anhydride during the racemization is 1 to 4 hours, preferably 2 to 3 hours.
Time. After the racemization reaction aging, the reaction solution is cooled, acid precipitated, and the crystals are separated, followed by ordinary post-treatments such as washing with water to obtain the desired product.

【0010】[0010]

【実施例】以下、本発明を実施例および比較例によりさ
らに詳しく説明する。 実施例1 300gの水に102.1g(0.5モル)のL−トリ
プトファンと44.4g(0.5モル)の45%NaO
H水溶液を加え、反応温度40℃で53.1g(0.5
2モル)の無水酢酸と53.5g(0.6モル)の45
%NaOHを同時に反応し、連続添加する。反応期間中
の溶液のpHを11〜13に保ち、二つの溶液の添加を
2.5時間で終了した。この反応液を液クロで分析する
と、N−アセチル−L−トリプトファンが123.1g
(アセチル化選択率の100%)であった。その反応液
を70℃に加熱し、153.1g(1.5モル)の無水
酢酸を2.5時間で添加後、5℃に冷却、濃塩酸を10
2.4g滴下し、濾過、水洗乾燥すると115.7gの
N−アセチル−DL−トリプトファンが得られた(L−
トリプトファンに対して94モル%)。〔比旋光度±
0.0(測定温度20℃)〕
The present invention will be described below in more detail with reference to Examples and Comparative Examples. Example 1 102.1 g (0.5 mol) of L-tryptophan and 44.4 g (0.5 mol) of 45% NaO in 300 g of water
H aqueous solution was added, and 53.1 g (0.5
2 mol) of acetic anhydride and 53.5 g (0.6 mol) of 45
% NaOH are reacted simultaneously and added continuously. The pH of the solution during the reaction period was maintained at 11-13, and the addition of the two solutions was completed in 2.5 hours. When this reaction solution was analyzed by liquid chromatography, 123.1 g of N-acetyl-L-tryptophan was obtained.
(100% of the acetylation selectivity). The reaction solution was heated to 70 ° C., 153.1 g (1.5 mol) of acetic anhydride was added over 2.5 hours, cooled to 5 ° C., and concentrated hydrochloric acid was added at 10 ° C.
2.4 g was dropped, filtered, washed with water and dried to obtain 115.7 g of N-acetyl-DL-tryptophan (L-
94 mol% based on tryptophan). (Specific rotation ±
0.0 (measuring temperature 20 ° C)]

【0011】比較例1 300gの水に102.1g(0.5モル)のL−トリ
プトファンと97.9g(1.1モル)の45%NaO
H水溶液を加えた溶液に、53.1g(0.52モル)
の無水酢酸を加え、反応温度40℃に保ちアセチル化の
反応を2.5時間で終了した。この反応液を液クロで分
析すると、N−アセチル−L−トリプトファンが98.
4g(アセチル化選択率の80%)であり、その反応液
を5℃に冷却して濃塩酸120.5gを滴下、濾過、水
洗乾燥すると91.6gのN−アセチル−L−トリプト
ファンが得られた(L−トリプトファンに対して74.
4モル%)。
Comparative Example 1 102.1 g (0.5 mol) of L-tryptophan and 97.9 g (1.1 mol) of 45% NaO in 300 g of water
53.1 g (0.52 mol) was added to the solution to which the H aqueous solution was added.
Acetic anhydride was added, and the reaction temperature was kept at 40 ° C., and the acetylation reaction was completed in 2.5 hours. When this reaction solution was analyzed by liquid chromatography, N-acetyl-L-tryptophan was 98.
4 g (80% of the acetylation selectivity). The reaction solution was cooled to 5 ° C., 120.5 g of concentrated hydrochloric acid was added dropwise, filtered, washed with water and dried to obtain 91.6 g of N-acetyl-L-tryptophan. (74 to L-tryptophan).
4 mol%).

【0012】比較例2 比較例1で得られたN−アセチル−L−トリプトファン
を250gの水と72.7g(0.82モル)の45%
NaOH水溶液を加え、反応温度40℃で、114.0
g(1.1モル)の無水酢酸を2.5時間で添加し、5
℃に冷却後、濃塩酸を81.1g滴下し、濾過、水洗乾
燥すると86.1gのN−アセチル−DL−トリプトフ
ァンが得られた(L−トリプトファンに対して69.9
モル%)〔比旋光度+4.3(測定温度20℃)〕。
Comparative Example 2 N-acetyl-L-tryptophan obtained in Comparative Example 1 was mixed with 250 g of water and 72.7 g (0.82 mol) of 45%
An aqueous NaOH solution was added, and at a reaction temperature of 40 ° C., 114.0.
g (1.1 mol) of acetic anhydride in 2.5 hours
After cooling to 0 ° C., 81.1 g of concentrated hydrochloric acid was added dropwise, followed by filtration, washing with water and drying, to obtain 86.1 g of N-acetyl-DL-tryptophan (69.9 g with respect to L-tryptophan).
Mol%) [specific optical rotation + 4.3 (measuring temperature 20 ° C)].

【0013】比較例3 L−トリプトファン40g(0.195モル)を1N
NaOH水溶液400mlに溶解し、無水酢酸130g
を6回に分けて滴下装入し激しく撹拌した。その後、反
応液を35〜40℃に保ち同温度で3時間撹拌した。し
ばらくすると結晶が析出した反応液を5℃に冷却し結晶
を濾過にて分離した。得られた結晶は水、希塩酸、水の
順に洗浄した。乾燥後N−アセチル−DL−トリプトフ
ァン36gを得た(L−トリプトファンより75モル
%)。mp204〜205℃
Comparative Example 3 40 g (0.195 mol) of L-tryptophan was added to 1N
Dissolved in 400 ml of NaOH aqueous solution, 130 g of acetic anhydride
Was added dropwise in six portions and stirred vigorously. Thereafter, the reaction solution was kept at 35 to 40 ° C and stirred at the same temperature for 3 hours. After a while, the reaction solution in which crystals precipitated was cooled to 5 ° C., and the crystals were separated by filtration. The obtained crystals were washed with water, diluted hydrochloric acid and water in this order. After drying, 36 g of N-acetyl-DL-tryptophan was obtained (75 mol% based on L-tryptophan). mp 204-205 ° C

【0014】[0014]

【発明の効果】本発明の方法により不純物の副生を抑制
し、アセチル化の反応率を向上させ高品質、高収率でN
−アセチル−L−トリプトファンを得、引き続き均一状
態でラセミ化する事により高品質、高収率で目的物を得
る事が出来工業的に有用な方法である。
According to the method of the present invention, by-products of impurities are suppressed, the reaction rate of acetylation is improved, and N is produced with high quality and high yield.
-Acetyl-L-tryptophan is obtained and subsequently racemized in a uniform state, whereby the desired product can be obtained in high quality and high yield, which is an industrially useful method.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 L−トリプトファンをアルカリ水溶液中
で無水酢酸と反応させN−アセチル−DL−トリプトフ
ァンを製造する方法に於いて、L−トリプトファン及び
L−トリプトファンに対しモル量のアルカリ金属水酸
化物の水溶液に該水溶液のpHを11以上に保ちなが
ら、無水酢酸とアルカリ金属水酸化物水溶液を同時に加
えてアセチル化を行い、引き続き水溶液を加熱下、更に
無水酢酸で処理する事を特徴とするN−アセチル−DL
−トリプトファンの製造方法。
1. A L- tryptophan In the process for producing N- acetyl -DL- tryptophan is reacted with acetic anhydride in an alkaline aqueous solution, L- tryptophan and L- tryptophan alkali metal hydroxide equimolar amount to The acetylation is performed by simultaneously adding acetic anhydride and an aqueous solution of an alkali metal hydroxide to the aqueous solution of the product while maintaining the pH of the aqueous solution at 11 or more, followed by further treating the aqueous solution with acetic anhydride while heating. N-acetyl-DL
-A method for producing tryptophan.
【請求項2】 アセチル化後の加熱温度が60〜100
℃、更に使用する無水酢酸の量がL−トリプトファンに
対し2〜5倍モルである請求項1記載の方法。
2. The heating temperature after acetylation is 60 to 100.
The method according to claim 1, wherein the amount of acetic anhydride used is 2 to 5 times mol of L-tryptophan.
JP21016192A 1992-08-06 1992-08-06 Method for producing N-acetyl-DL-tryptophan Expired - Fee Related JP3229658B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21016192A JP3229658B2 (en) 1992-08-06 1992-08-06 Method for producing N-acetyl-DL-tryptophan

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21016192A JP3229658B2 (en) 1992-08-06 1992-08-06 Method for producing N-acetyl-DL-tryptophan

Publications (2)

Publication Number Publication Date
JPH0656775A JPH0656775A (en) 1994-03-01
JP3229658B2 true JP3229658B2 (en) 2001-11-19

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Country Link
JP (1) JP3229658B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63212681A (en) * 1987-02-26 1988-09-05 Murata Mach Ltd Winding control method in automatic winder

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