JPS6012343B2 - Method for isolating cystine or cysteine and tyrosine - Google Patents

Method for isolating cystine or cysteine and tyrosine

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Publication number
JPS6012343B2
JPS6012343B2 JP7027682A JP7027682A JPS6012343B2 JP S6012343 B2 JPS6012343 B2 JP S6012343B2 JP 7027682 A JP7027682 A JP 7027682A JP 7027682 A JP7027682 A JP 7027682A JP S6012343 B2 JPS6012343 B2 JP S6012343B2
Authority
JP
Japan
Prior art keywords
cystine
tyrosine
cysteine
crystals
isolating
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
JP7027682A
Other languages
Japanese (ja)
Other versions
JPS58188846A (en
Inventor
浩猛 尾上
祐三 山本
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 RIKAGAKU YAKUHIN KK
Original Assignee
NIPPON RIKAGAKU YAKUHIN 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 NIPPON RIKAGAKU YAKUHIN KK filed Critical NIPPON RIKAGAKU YAKUHIN KK
Priority to JP7027682A priority Critical patent/JPS6012343B2/en
Publication of JPS58188846A publication Critical patent/JPS58188846A/en
Publication of JPS6012343B2 publication Critical patent/JPS6012343B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 シスチンおよびチロジンの製造は、従来、人髪、羽毛等
のシスチンを多量に含むたんぱく質を鉱酸で加水分解し
、その分解液にアルカリを加えて中和して析出した簸溶
性アミノ酸混合物を炉別したのち個々のアミノ酸を単離
している。
[Detailed Description of the Invention] Conventionally, cystine and tyrosine have been produced by hydrolyzing proteins containing large amounts of cystine such as human hair and feathers with mineral acids, and adding an alkali to the decomposition solution to neutralize it and precipitate it. Individual amino acids are isolated after elutriation-soluble amino acid mixtures are separated.

簸溶性アミノ酸混合物中に含まれるシスチン及びチロジ
ンは、餌の変化により種々の挙動を示す。雛溶性アミノ
酸混合物を雛酸に溶かし、アルカリを加えて斑1〜2に
調整するときはシスチンのみが析出し、また雛溶性アミ
/酸をアルカリに溶かし、酸を加えてpH9〜10に調
整するときはチロジンのみが析出する。これらの性質は
それらの工業的製造法にも利用されている。しかしなが
ら、これらの方法で抽出し得るシスチン及びチロジンは
、簸溶性アミノ酸混合物中の含有量に対してシスチンで
は80〜85%、チロジンでは40〜50%が抽出され
るにすぎない。また、難綾性アミ/酸混合物中のシスチ
ンとチロジンの比率によっても影響がある。特に肉1〜
2の領域では、シスチンの比率が高い場合は問題はない
が、チロジンの比率が高くなるとシスチンと共にチロジ
ンも析出して分離が困難になる。本発明によると、シス
チンとチロジンの比率とは無関係に両者を分離すること
ができ、また場合によってはシスチンの還元体であるシ
ステインを得ることもできる。
Cystine and tyrosine contained in the elutriophilic amino acid mixture exhibit various behaviors depending on changes in feed. When a chick-soluble amino acid mixture is dissolved in chick acid and adjusted to a pH of 1 to 2 by adding an alkali, only cystine precipitates, and when a chick-soluble amino acid/acid is dissolved in an alkali and an acid is added to adjust the pH to 9 to 10. In this case, only tyrosine precipitates. These properties are also utilized in their industrial manufacturing methods. However, cystine and tyrosine can be extracted by these methods, and only 80 to 85% of cystine and 40 to 50% of tyrosine are extracted based on the content in the elutri-soluble amino acid mixture. It is also influenced by the ratio of cystine to tyrosine in the amine/acid mixture. Especially meat 1~
In the region 2, there is no problem when the ratio of cystine is high, but when the ratio of tyrosine is high, tyrosine is precipitated together with cystine, making separation difficult. According to the present invention, cystine and tyrosine can be separated regardless of their ratio, and in some cases, cysteine, which is a reduced form of cystine, can be obtained.

シスチン及びチロジンは、アミノ酸中で両者共に最も溶
解度が低く、シスチンは2尊0において水100の【中
11.2磯、チロジンは25℃において水100の【中
45.物2カ【溶解するに過ぎない。
Cystine and tyrosine both have the lowest solubility among amino acids, with cystine having the lowest solubility of 11.2% in 100% of water at 2% and tyrosine having the lowest solubility of 45% in 100% of water at 25°C. 2 things [it just dissolves].

両者の混合物を分離するには、どちらか一方を易溶性に
変えて溶解度差を利用すれば良い。シスチン(1)は、
次式の如く、還元するとき容易にシステイン(0)を生
成し、システインは空気酸化等の弱い酸化条件でも、ま
た過酸化水素等の酸化剤によっても容易に酸化してシス
チンに戻すことができる。
In order to separate a mixture of the two, it is sufficient to make one of them easily soluble and utilize the solubility difference. Cystine (1) is
As shown in the following formula, cysteine (0) is easily generated during reduction, and cysteine can be easily oxidized and returned to cystine even under weak oxidizing conditions such as air oxidation, or by oxidizing agents such as hydrogen peroxide. .

またシスティンは水に溶けやすい。Also, cysteine is easily soluble in water.

本発明者はこの特性を利用して次の方法によりシスチン
及びチロジンの分離を試みた。
The present inventor took advantage of this property and attempted to separate cystine and tyrosine by the following method.

Lーシスチン及びLーチロジンの混合物を塩酸に溶かし
陰極液とする。
A mixture of L-cystine and L-tyrosine is dissolved in hydrochloric acid to prepare a catholyte.

また陽極液は5%硫酸液を用い、賜イオン交換膜を隔膜
として、陰極液及び陽極液中に白金電極を浸し〜直流電
流を通じて還元を行なう。陰極液は、薄層クロマトグラ
フィによりLーシスチンが完全にL−システィンに濠元
されたことを確認したのち「アンモニア水を滴下してp
Hを5に調整し「析出した結晶(L−チロジン)を炉則
して回収する。また炉液にはニトロブルシド試液により
青色を発しなくなるまで過酸化水素水を滴下して酸化す
る。析出した結晶が溶けるまで塩酸を加え、アンモニア
水を滴下してPHを2.5とし、再び析出した結晶(L
ーシスチソ)を炉別して回収する。これにより得られた
結果を第1表に示す。第 1 表 この実験に用いたLーシスチンは比旋光度〔Q〕色。
A 5% sulfuric acid solution is used as the anolyte, and a platinum electrode is immersed in the catholyte and anolyte using an ion-exchange membrane as a diaphragm, and reduction is carried out through direct current. After confirming that L-cystine was completely converted into L-cystine by thin layer chromatography, the catholyte was prepared by adding aqueous ammonia dropwise.
Adjust H to 5 and collect the precipitated crystals (L-tyrosine) according to the furnace rules.Additionally, hydrogen peroxide solution is added dropwise to the furnace liquid until it no longer emits blue color using a nitrobrucid test solution to oxidize the precipitated crystals. Add hydrochloric acid until dissolved, add aqueous ammonia dropwise to adjust the pH to 2.5, and re-precipitate crystals (L
Cystiso) is separated from the furnace and collected. The results obtained are shown in Table 1. Table 1 L-cystine used in this experiment has specific rotation [Q] color.

一221.70及び含量は99.8%(ヨウ素滴定法)
、Lーチロジンは比旋光度〔Q〕登0一11.60及び
含量は99.2%(マクロゲルダール法)のものを用い
たが、回収率、光学純度及び含量のいずれも満足すべき
結果であり、優れた単離法であることが確認された。次
に、実際にたんぱく質を用いた実施例を説明する。
-221.70 and content is 99.8% (iodine titration method)
, L-tyrosine with a specific optical rotation [Q] of 0-11.60 and a content of 99.2% (Macrogerdal method) was used, and the results were satisfactory in terms of recovery rate, optical purity, and content. It was confirmed that this is an excellent isolation method. Next, an example in which a protein is actually used will be explained.

実施例 1 にわとりの羽毛3k9に磯‐塩酸6そを加え、還流冷却
しながら8時間加熱して加水分解をする。
Example 1 Six pieces of seaweed-hydrochloric acid are added to 3k9 chicken feathers, and the mixture is heated under reflux for 8 hours for hydrolysis.

加水分解液を冷却して苛性ソーダ液(20%)でpH5
.0に調整し、生じた沈澱を炉過する。炉取した沈澱物
に水3.5そ及び塩酸800泌を加えて溶かし、活性炭
を加えて脱色炉過する。炉液にかきまぜながら、アンモ
ニア水を滴下してpHを4.5〜5.5に調整すると、
結晶が析出する。結晶を炉過して乾燥すると、その収量
は255夕であった。
Cool the hydrolyzed solution and adjust the pH to 5 with caustic soda solution (20%).
.. 0 and filter the resulting precipitate. 3.5 parts of water and 800 parts of hydrochloric acid are added to the precipitate collected in the oven to dissolve it, and activated carbon is added and filtered for decolorization. While stirring the furnace liquid, add ammonia water dropwise to adjust the pH to 4.5 to 5.5.
Crystals precipitate. The crystals were filtered and dried and the yield was 255 kg.

この結晶混合物中に含まれるシスチンは63%及びチロ
ジンは31%であり、その他のアミノ酸は僅少量であっ
た。この結晶混合物に洲−塩酸800の‘を加えて溶か
して「陰極液とする。
This crystal mixture contained 63% cystine and 31% tyrosine, and only small amounts of other amino acids. Add 800% of Su-HCl to this crystal mixture and dissolve it to form a catholyte.

また陽極液は5%硫酸900の‘を用いt腸イオン交換
膜0.1力を隅膜として〜陰極液中には銀板電極、陽極
液中には炭素板電極を浸して陽イオン交換膜ldめ当り
IAの直流電流を通じて電解還元を行なう。陰極液は薄
層クロマトグラフイによりシスチンが完全にシスティン
に還元されたことを確認したのちにとり出しt よくか
きまぜながらアンモニア水を滴下してpHを5.0に調
整すると結晶が析出する。この結晶を炉別(炉液は保存
)し、アンモニア水500泌に溶かして活性炭を加えて
炉過した炉液を減圧濃縮することにより析出した結晶を
炉遇して乾燥すると、その収量は54.6夕であった。
In addition, the anolyte is 5% sulfuric acid 900%, and the cation exchange membrane is 0.1 strength as the corneal membrane.A silver plate electrode is immersed in the catholyte, and a carbon plate electrode is immersed in the anolyte. Electrolytic reduction is performed through direct current of IA per ld. After confirming that cystine has been completely reduced to cysteine by thin layer chromatography, the catholyte is taken out. While stirring well, aqueous ammonia is added dropwise to adjust the pH to 5.0, and crystals are precipitated. The crystals were separated in a furnace (the furnace liquid was saved), dissolved in 500 g of aqueous ammonia, activated carbon was added, and the furnace liquid was concentrated under reduced pressure. The precipitated crystals were then dried in a furnace. It was 6th evening.

結晶は針状で、比旋光度〔Q〕色。‐11.斑o 、C
:59.6%、N:7。69%であり、Lーチロジンに
一致した。
The crystals are needle-shaped and have a specific rotation [Q] color. -11. Spots o, C
:59.6%, N:7.69%, which corresponded to L-tyrosine.

回収率は結晶混合物中のチロジンより換算して69%で
ある。また、前記の保存炉液をよく額梓、冷却しながら
、ニトロプルシド謎液により青色を呈しなくなるまで過
酸化水素水を滴下したのち、析出した結晶に塩酸160
の‘を加えて溶かし、活性炭を加えて脱色炉遇した炉液
をよく鷹拝しながらアンモニア水を滴下して州2.5に
調整すると、結晶が析出する。
The recovery rate was 69% based on tyrosine in the crystal mixture. In addition, while cooling the storage solution well, hydrogen peroxide solution was added dropwise until the nitroprusside mysterious solution no longer showed blue color, and then hydrochloric acid 160% was added to the precipitated crystals.
If you add aqueous ammonia and adjust the temperature to 2.5, crystals will precipitate out.

析出した結晶を炉過、乾燥して得られる収量は157夕
であった。この結晶は、比旋光度〔Q〕蟹一221.9
0 、C:29.7%、N:11.58%であり、Lー
シスチンに一致した。回収率は結晶混合物中のシスチン
より換算して97.7%であった。実施例 2人髪3k
9を用い、実施例1と同様に加水分解及びpH調整を行
ない、混合結晶346夕を得た。
The yield obtained by filtering and drying the precipitated crystals was 157 pieces. This crystal has a specific optical rotation [Q] of 221.9
0, C: 29.7%, N: 11.58%, which corresponded to L cystine. The recovery rate was 97.7% based on cystine in the crystal mixture. Example 2 people hair 3k
9, hydrolysis and pH adjustment were carried out in the same manner as in Example 1 to obtain 346 mixed crystals.

混合結晶中に含まれるシスチンは78%、チロジンは1
7.6%であった。この混合結晶を実施例1と同機に電
解還元及び結晶化を行なうとき、L−チロジン43.2
夕(〔Q〕旨。
The mixed crystal contains 78% cystine and 1 tyrosine.
It was 7.6%. When this mixed crystal was subjected to electrolytic reduction and crystallization in the same machine as in Example 1, L-tyrosine 43.2
Evening ([Q] effect.

−11‐210・C:59‐62%、N:7‐71%)
を得た。回収率は結晶混合物より換算して72%である
。またL−シスチンは2629(〔Q〕色0一220.
950、C:29.73%、N;11.61%)を得た
。回収率は結晶混合物中のシスチンより換算して97%
である。実施例 3 人髪3k9を用い、実施例1と同様に加水分解及びpH
調整を行ない、混合結晶330夕を得た。
-11-210・C: 59-62%, N: 7-71%)
I got it. The recovery rate is 72% calculated from the crystal mixture. Also, L-cystine is 2629 ([Q] color 0-220.
950, C: 29.73%, N: 11.61%). Recovery rate is 97% based on cystine in the crystal mixture
It is. Example 3 Using human hair 3k9, hydrolysis and pH adjustment were carried out in the same manner as in Example 1.
After adjustment, 330 pieces of mixed crystals were obtained.

混合結晶中に含まれるシスチンは78.6%、チロジン
は16.9%であった。この混合結晶を実施例1と同様
に電解還元及び結晶化(但し、保存炉液は別に処理)す
るとき、Lーチロジン41.8夕(〔Q〕啓一11.3
20、C:59.52%、N:7.58%)が得られた
The mixed crystal contained 78.6% cystine and 16.9% tyrosine. When this mixed crystal was subjected to electrolytic reduction and crystallization in the same manner as in Example 1 (however, the storage solution was treated separately), L-tyrosine 41.8 hours ([Q] Keiichi 11.3
20, C: 59.52%, N: 7.58%) was obtained.

Claims (1)

【特許請求の範囲】[Claims] 1 シスチンとチロジンとを含む混合物を鉱酸に溶解し
、溶液中のシスチンを電解還元してシステインに変換さ
せた後、アルカリを加えて中和し、析出するチロジンを
濾別採取し、濾液を濃縮してシステインを析出分離する
か、または濾液中のシステインを酸化してシスチンとし
て回収することを特徴とするシスチンまたはシステイン
およびチロジンの単離法。
1 Dissolve a mixture containing cystine and tyrosine in mineral acid, electrolytically reduce the cystine in the solution to convert it to cysteine, neutralize it by adding an alkali, collect the precipitated tyrosine by filtration, and collect the filtrate. A method for isolating cystine or cysteine and tyrosine, which comprises concentrating to precipitate and separate cysteine, or oxidizing cysteine in the filtrate and recovering it as cystine.
JP7027682A 1982-04-28 1982-04-28 Method for isolating cystine or cysteine and tyrosine Expired JPS6012343B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7027682A JPS6012343B2 (en) 1982-04-28 1982-04-28 Method for isolating cystine or cysteine and tyrosine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7027682A JPS6012343B2 (en) 1982-04-28 1982-04-28 Method for isolating cystine or cysteine and tyrosine

Publications (2)

Publication Number Publication Date
JPS58188846A JPS58188846A (en) 1983-11-04
JPS6012343B2 true JPS6012343B2 (en) 1985-04-01

Family

ID=13426820

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7027682A Expired JPS6012343B2 (en) 1982-04-28 1982-04-28 Method for isolating cystine or cysteine and tyrosine

Country Status (1)

Country Link
JP (1) JPS6012343B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101023538B1 (en) * 2009-01-22 2011-03-21 (주)해림파메틱 A method of producing L-Cystine
WO2023190689A1 (en) * 2022-03-30 2023-10-05 富士フイルム株式会社 Method for producing mixed powder, mixed powder, powder, and powder culture medium

Also Published As

Publication number Publication date
JPS58188846A (en) 1983-11-04

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