Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS6036440B2 - Production method of pyroglutamylglycine - Google Patents
[go: Go Back, main page]

JPS6036440B2 - Production method of pyroglutamylglycine - Google Patents

Production method of pyroglutamylglycine

Info

Publication number
JPS6036440B2
JPS6036440B2 JP8288277A JP8288277A JPS6036440B2 JP S6036440 B2 JPS6036440 B2 JP S6036440B2 JP 8288277 A JP8288277 A JP 8288277A JP 8288277 A JP8288277 A JP 8288277A JP S6036440 B2 JPS6036440 B2 JP S6036440B2
Authority
JP
Japan
Prior art keywords
pyroglutamylglycine
glycine
reaction
glutamic acid
selectivity
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
JP8288277A
Other languages
Japanese (ja)
Other versions
JPS5419968A (en
Inventor
長三 井上
強 山田
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.)
Resonac Holdings Corp
Original Assignee
Showa Denko KK
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 Showa Denko KK filed Critical Showa Denko KK
Priority to JP8288277A priority Critical patent/JPS6036440B2/en
Publication of JPS5419968A publication Critical patent/JPS5419968A/en
Publication of JPS6036440B2 publication Critical patent/JPS6036440B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Peptides Or Proteins (AREA)

Description

【発明の詳細な説明】 本発明はピログルタミルグリシンの製造法に関する。[Detailed description of the invention] The present invention relates to a method for producing pyroglutamylglycine.

ピログルタミルグリシンはガストリンなどの生理活性べ
プチドの前駆体として供給される(J.Chem.So
c.C.1967.2410)他に、それ自体、抗菌性
、保温性等を併せ持つ物質であるので化粧品用等の用途
を有する物質である。
Pyroglutamylglycine is supplied as a precursor of bioactive peptides such as gastrin (J. Chem. So
c. C. 1967.2410) In addition, since it is a substance that itself has antibacterial properties, heat retention properties, etc., it has uses such as cosmetics.

グルタミン酸(もしくはピログルタミン酸)とグリシン
とを混合して、ピログルタミン酸の融点付近の温度で加
熱すると、グリシンが速に溶解し、ジベプチド、トリベ
プチド、テトラベプチドなどが生成し、また原料のグリ
シンの割合が増大したり、反応時間が長いときには、水
に不溶性のポリマー状のポリベプチドが生成してしまう
ことが知られている。
When glutamic acid (or pyroglutamic acid) and glycine are mixed and heated at a temperature near the melting point of pyroglutamic acid, glycine quickly dissolves, producing dipeptide, tribeptide, tetrabeptide, etc., and the proportion of glycine in the raw material increases. It is known that when the reaction time is too long, a water-insoluble polymeric polypeptide is produced.

この際、トリベプチドやテトラベプチドの副生防止を図
るため、グリシンの使用割合を低めたり、反応時間を低
くすることもなし得るが、その場合には、転化率や収率
が著しく低下したり、反応時間が著しく長びくという不
利点を伴うこととなり、いずれにしても、ピログルタミ
ルグリシンの選択的生成を招く手段とは成り難いもので
あった。本発明者等はグルタミン酸(もしくはピログル
タミン酸)とグリシンとを熱縮合させる際にアセトフェ
ノンの存在の下で、反応を行うことにより、ジベプチド
、トリベプチド等の高次のべプチドの副生を抑制しピロ
グルタミルグリシンを選択的に生成させることができる
ことを見出した。
At this time, in order to prevent the by-product of tribeptide and tetrabeptide, it is possible to reduce the proportion of glycine used or to shorten the reaction time, but in that case, the conversion rate and yield may drop significantly, or the reaction time may be reduced. This has the disadvantage that it takes a considerable amount of time, and in any case, it cannot be used as a means for selectively producing pyroglutamylglycine. The present inventors conducted the thermal condensation of glutamic acid (or pyroglutamic acid) and glycine in the presence of acetophenone, thereby suppressing the by-products of higher peptides such as dipeptide and tribeptide, and suppressing the by-product of higher peptides such as dipeptide and tribeptide. It has been found that glutamylglycine can be selectively produced.

本発明はかかる知見に基づくものである。本発明方法に
おいて原料として用いるグルタミン酸は加熱により容易
にピログルタミン酸となるため、両者はいずれを用いて
も同一の結果を招来する。
The present invention is based on this knowledge. Since the glutamic acid used as a raw material in the method of the present invention is easily converted into pyroglutamic acid by heating, the same result will be obtained no matter which one is used.

本発明方法においては、原料グルタミン酸とグリシンの
使用割合は化学量論量にて行うことが好ましいが、転化
率向上のためグリシンを若干過剰に用いても良い。
In the method of the present invention, the raw materials glutamic acid and glycine are preferably used in stoichiometric amounts, but glycine may be used in slightly excess to improve the conversion rate.

通常は1:1〜1:5(モル比)の範囲で行うことが適
当である。アセトフェノンは、原料の少くとも5重量%
程度の量で使用するのが好ましい。
Usually, it is appropriate to carry out the reaction in a range of 1:1 to 1:5 (molar ratio). Acetophenone is at least 5% by weight of the raw material
It is preferable to use it in a moderate amount.

多量に用いても反応自体には悪影響を及ぼさないため必
要に応じて溶媒を兼ねて用いても良い。反応時間は通常
は130〜200qCであり、反応時間は10〜6び分
(好ましくは3び分以下)である。反応は不活性ガス例
えば窒素、炭酸ガス等の雰囲気中で行うのが望ましい。
Even when used in a large amount, it does not adversely affect the reaction itself, so it may also be used as a solvent if necessary. The reaction time is usually 130 to 200 qC, and the reaction time is 10 to 6 minutes (preferably 3 minutes or less). The reaction is preferably carried out in an atmosphere of an inert gas such as nitrogen or carbon dioxide.

反応中に発生する水蒸気は連続的に取り除くことができ
るが、これは実施上の必須条件ではない。本発明方法に
より得られたピログルタミルグリシンは水溶液とし、イ
オン交灘樹脂を通すことにより、創生物や未反応アミノ
酸と容易に分離し得る。
The water vapor generated during the reaction can be removed continuously, but this is not a practical requirement. Pyroglutamylglycine obtained by the method of the present invention can be easily separated from created substances and unreacted amino acids by making it into an aqueous solution and passing it through an ion exchange resin.

ピログルタミルグリシンの如き簡単な構造のジベフ。Dibef with a simple structure such as pyroglutamylglycine.

チドですら、既存の合成法によっては、高価、複雑な工
程を経て、製造しなければならないのに対し、本発明方
法においては以上、述べた如く簡易な操作で、著しく高
い選択的生成率をもってピログルタミルグリシンを製造
することができるので実用上極めて優れた価値を有する
方法である。以下、実施例ならびに比較例により本発明
を説明する。
Although even tide must be produced through expensive and complicated steps using existing synthesis methods, the method of the present invention can be produced with extremely high selective production rates through simple operations as described above. This method has extremely high practical value because it can produce pyroglutamylglycine. The present invention will be explained below with reference to Examples and Comparative Examples.

実施例 1グルタミン酸とグリシンを1:1モル比に混
合して、炭酸ガスで置換したガラス反応管中に入れ、ア
セトフェノン1の重量%を添加したのち、ガラス管を熔
封する。
Example 1 Glutamic acid and glycine were mixed at a molar ratio of 1:1, placed in a glass reaction tube purged with carbon dioxide gas, and after adding 1% by weight of acetophenone, the glass tube was sealed.

このガラス封管をオイルバス中で1750030分間反
応させたところ、グルタミン酸の転化率は40.4%、
ピログルタミルグリシンの選択率は78%であった。そ
の他、ピログルタミルグリシルグリシンの生成率は2.
2%、ピログルタミルグリシルグリシルグリシンの生成
率は0.6%であり、グリシンのみのべプチド、グリシ
ンの環状二量体の生成は微々たるものであった。比較例
1 ■ グルタミン酸とグリシンを1:1モル比に混合して
、アセトフェノンを加えずに上記と全く同様の反応を行
ったところ、ピログルタミルグ1Jシンの選択率は64
%であった。
When this glass sealed tube was reacted for 1,750,030 minutes in an oil bath, the conversion rate of glutamic acid was 40.4%.
The selectivity for pyroglutamylglycine was 78%. In addition, the production rate of pyroglutamylglycylglycine is 2.
The production rate of pyroglutamylglycylglycylglycine was 0.6%, and the production of glycine-only peptides and glycine cyclic dimers was negligible. Comparative Example 1 ■ When glutamic acid and glycine were mixed in a 1:1 molar ratio and the same reaction as above was carried out without adding acetophenone, the selectivity for pyroglutamyl glutamine was 64.
%Met.

ピログルタミルグリシルグリシン、ピログルタミルグリ
シルグリシルグリシンの収率はそれぞれ4.6%、2.
5%に増加し、グリシンのみのべプチドやジケトピベラ
ジンの副生の増加がみとめられた。■ グルタミン酸と
グリシンを1:1モル比に混合して、反応温度を90℃
に下げて反応を行ったところ、ピログルタミルグリシン
の収率10%選択率80%に達するのに10加持間を要
した。
The yields of pyroglutamylglycylglycine and pyroglutamylglycylglycylglycine were 4.6% and 2.
5%, and an increase in by-products of glycine-only peptides and diketopiverazine was observed. ■ Mix glutamic acid and glycine in a 1:1 molar ratio and raise the reaction temperature to 90℃.
When the reaction was carried out at a lower temperature, it took 10 hours to reach a yield of pyroglutamylglycine of 10% and a selectivity of 80%.

実施例 2グルタミン酸とグリシンを1:1.5モル比
に混合して、アセトフェノン1の重要%添加し、実施例
1と全く同様にして、175℃3び分の反応を行ったと
ころピログルタミルグリシンの選択率は77%であった
Example 2 Glutamic acid and glycine were mixed at a molar ratio of 1:1.5, a significant percentage of acetophenone was added, and the reaction was carried out for 3 times at 175°C in exactly the same manner as in Example 1, resulting in pyroglutamylglycine. The selectivity was 77%.

その他、ピログルタミルグリシルグリシン2.4%、ピ
ログルタミルグリシルグリシルグリシン0.7%の収率
であった。(グルタミン酸の転化率45%)比較例 2 ■ アセトフェノン無添加で上記と全く同様の反応を行
ったところ、ピログルタミルグリシンの選択率は55%
であり、ピログルタミルグリシルグリシンは6.9%収
率、ピログルタミルグリシルグリシルグリシンは3.6
%と増加した。
In addition, the yield was 2.4% of pyroglutamylglycylglycine and 0.7% of pyroglutamylglycylglycylglycine. (Conversion rate of glutamic acid 45%) Comparative example 2 ■ When the same reaction as above was carried out without adding acetophenone, the selectivity of pyroglutamylglycine was 55%.
The yield of pyroglutamylglycylglycine is 6.9%, and the yield of pyroglutamylglycylglycylglycine is 3.6%.
%.

この反応において、4ーメチルアセトフェノン、プロピ
オフェノンの添加効果も試みたが、収率、選択率になん
らの変化もみとめられなかつた。■ グルタミン酸とグ
リシンの混合モル比を4:1に変えて、同様の反応を行
ったところ、ピログルタミルグリシンの選択率は80%
であったが、転化率(グルタミン酸)はわずか17%に
すぎなかった。
In this reaction, the effect of adding 4-methylacetophenone and propiophenone was also tried, but no change in yield or selectivity was observed. ■ When the same reaction was carried out with the molar ratio of glutamic acid and glycine changed to 4:1, the selectivity of pyroglutamylglycine was 80%.
However, the conversion rate (glutamic acid) was only 17%.

*反応生成物の分析は、0.1%日3P04水溶液とし
てShodexIonpacC−811カラムを用いる
高速液体クロマトグラフィーを用いて行ったものである
*Analysis of reaction products was performed using high performance liquid chromatography using a Shodex Ionpac C-811 column as a 0.1% aqueous solution of 3P04.

Claims (1)

【特許請求の範囲】[Claims] 1 グルタミン酸もしくはピログルタミン酸とグリシン
とをアセトフエノンの存在の下に加熱することを特徴と
するピログルタミルグリシンの製造法。
1. A method for producing pyroglutamylglycine, which comprises heating glutamic acid or pyroglutamic acid and glycine in the presence of acetophenone.
JP8288277A 1977-07-13 1977-07-13 Production method of pyroglutamylglycine Expired JPS6036440B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8288277A JPS6036440B2 (en) 1977-07-13 1977-07-13 Production method of pyroglutamylglycine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8288277A JPS6036440B2 (en) 1977-07-13 1977-07-13 Production method of pyroglutamylglycine

Publications (2)

Publication Number Publication Date
JPS5419968A JPS5419968A (en) 1979-02-15
JPS6036440B2 true JPS6036440B2 (en) 1985-08-20

Family

ID=13786636

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8288277A Expired JPS6036440B2 (en) 1977-07-13 1977-07-13 Production method of pyroglutamylglycine

Country Status (1)

Country Link
JP (1) JPS6036440B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1987005219A1 (en) * 1986-02-28 1987-09-11 Bio-Tech A/S Pharmaceutical preparation containing a dipeptide with cell growth regultating effect

Also Published As

Publication number Publication date
JPS5419968A (en) 1979-02-15

Similar Documents

Publication Publication Date Title
JPS60237030A (en) Manufacture of 1,2,3-trichloro-2-methyl-prone
JPS6036440B2 (en) Production method of pyroglutamylglycine
JPS5829757A (en) Production of optically active mandelonitrile
US3894097A (en) Process for the preparation of hexafluoroisobutylene
JPS6114144B2 (en)
JPS6035356B2 (en) Method for producing pyroglutamyl peptide
JPH107623A (en) Production of bis(trichloromethyl) carbonate
US3781346A (en) Process for purification of naphthalene carboxylic acids
HU185787B (en) Process for preparing benzoxazolone
US602109A (en) Israel rods
SU512210A1 (en) The method of producing potassium hydromelonate
US3781347A (en) Process for purification of terephthalic acid
JPS6157293B2 (en)
Su et al. A simple, novel method for the preparation of trifluoromethyl iodide and diiododifluoromethane
IL47643A (en) Oxidation of magnesium chloride
JP4326921B2 (en) Method for producing 3-buten-1-ol
JP3135660B2 (en) Method for producing perfluoro-oxyaziridine
SU364619A1 (en) METHOD OF OBTAINING CHLORINE DERIVATIVES OF PHENYLTRHNHLORHERMERMNA
SU438244A1 (en) The method of obtaining p-terphenyl
SU1330134A1 (en) Method of producing 5-phenylethynylfurfural
JPH08134038A (en) Production of carbazinic acid
JPH0338564A (en) Method for producing 4,4'-bis(4-aminophenylthio)diphenylsulfone
SU566818A1 (en) Method of producing monochloro derivatives of diphenyl ether
JPS6016431B2 (en) Fluorination method
JPS6036453A (en) Preparation of pentafluorobenzonitrile