JPS58188846A - Separation of cystine or cysteine and tyrosine - Google Patents

Separation of cystine or cysteine and tyrosine

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Publication number
JPS58188846A
JPS58188846A JP7027682A JP7027682A JPS58188846A JP S58188846 A JPS58188846 A JP S58188846A JP 7027682 A JP7027682 A JP 7027682A JP 7027682 A JP7027682 A JP 7027682A JP S58188846 A JPS58188846 A JP S58188846A
Authority
JP
Japan
Prior art keywords
cystine
tyrosine
solution
filtrate
catholyte
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.)
Granted
Application number
JP7027682A
Other languages
Japanese (ja)
Other versions
JPS6012343B2 (en
Inventor
Hirotake Onoe
浩猛 尾上
Yuzo Yamamoto
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
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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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Abstract

PURPOSE:To separate the titled substances from a mixture containing cystine and tyrosine, by dissolving the mixture in a mineral acid, converting the cystine in the solution to cysteine by reduction, neutralizing the solution with an alkali, separating the precipitated tyrosine by filtration, and concentrating the filtrate. CONSTITUTION:A mixture of L-cystine and L-tyrosine is dissolved in hydrochloric acid and the solution is used as the catholyte. The anolyte is 5% sulfuric acid solution, and a cation exchange membrane is used as the membrane. The catholyte is reduced by dipping platinum electrodes in the catholyte and the anolyte, and passing DC current through the membrane. After ascertaining the complete reduction of L-cystine to L-cysteine by thin-layer chromatography, the catholyte is adjusted to pH 5 by dripping ammonia water, and the precipitated crystal (L-tyrosine) is recovered by filtration. The filtrate is oxidized by adding hydrogen peroxide solution dropwise to the filtrate until the filtrate does not develop blue color by nitroprusside reagent. The oxidized filtrate is mixed with hydrochloric acid to dissolve the precipitated crystal, added ammonia water dropwise to attain 2.5pH, and the reprecipitated crystal (L-cystine) is recovered by filtration.

Description

【発明の詳細な説明】 シスチンおよびチロシ′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ば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難
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。難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、−の変化によシ種々の挙動を示す
。難溶性アミノ酸混合物を鉱酸に溶かし、アルカリを加
えて−l〜2に調整するときはシスチンのみが析出し、
また難溶性アミノ酸をアルカリに溶かし、酸を加えて−
9〜10に調整するときはチロシンのみが析出する。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
[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 then neutralizing the decomposition solution by adding an alkali. The precipitated poorly soluble amino acid mixture is separated in a furnace and then the individual amino acids are isolated. Cystine and tyrodine contained in the poorly soluble amino acid mixture exhibit various behaviors depending on the change in -. When a poorly soluble amino acid mixture is dissolved in mineral acid and adjusted to -1 to 2 by adding alkali, only cystine precipitates,
In addition, by dissolving poorly soluble amino acids in alkali and adding acid,
When adjusting to 9 to 10, only tyrosine is precipitated. These properties are also utilized in their industrial manufacturing methods.

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、難溶性アミノ酸混合物中の含有量に対し
てシスチンでは80〜859c、チロダンでは40〜5
0%が抽出されるにすぎない。
However, cystine and tyro-zine that can be extracted by these methods are 80 to 859 c for cystine and 40 to 5 for tyrodane, relative to the content in the sparingly soluble amino acid mixture.
Only 0% is extracted.

マタ、難溶性アミノ酸混合物中のシスチンとチロシンの
比率によっても影響がある。特に−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、チロシンの
比率が高くなるとシスチンと共にチロシンも析出して分
離が困難になる。
The ratio of cystine to tyrosine in the poorly soluble amino acid mixture also has an effect. Especially in the area of -1 to 2,
If the ratio of cystine is high, there is no problem, but if the ratio of tyrosine is high, tyrosine will precipitate along with cystine, making separation difficult.

本発明によると、シスチンとチロシ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ィンを得るとともできる。
According to the present invention, cystine and tyrosine can be separated regardless of their ratio, and in some cases, cystine, which is a reduced form of cystine, can be obtained.

シスチン及びチロダンは、アミノ酸中で両者共に最も溶
解度が低く、シスチンは25℃において水1ooWd中
11.219.チロシンは25℃において水lO〇−中
45.319が溶解するに過ぎない。
Cystine and tyrodane both have the lowest solubility among the amino acids, with cystine having the lowest solubility in 1 ooWd of water at 25°C. Tyrosine dissolves in only 45.319 ml of water at 25°C.

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。
In order to separate a mixture of the two, it is sufficient to make one of them easily soluble and utilize the solubility difference.

シスチン(1)は、次式の如く、還元するとき容易にシ
スティン(1)を生成し、システィ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。
Cystine (1) easily generates cystine (1) when reduced, as shown in the following formula, and cystine is easily oxidized even under weak oxidizing conditions such as air oxidation or by oxidizing agents such as hydrogen peroxide. Can be converted back to cystine.

(1)         (1) またシスティンは水に溶けやすい。(1) (1) 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
及びチロシンの分離を試みた。
The present inventor took advantage of this property and attempted to separate cystine and tyrosine by the following method.

L−シスチン及びL−チロシンの混合物を塩酸に溶かし
陰極液とする。また陽極液は5%硫酸液′を用い、陽イ
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シム−シスチンが完全にL−
システィンに還元されたことを確認したのち、アンモニ
ア水を滴下して−を5に調整し、析出した結晶(L−チ
ロ・ジ′ン)を戸別して回収する。またろ液にはニトロ
プ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−を2.5とし、再び
析出した結晶(L−シスチン)をい別して回収する。こ
れにより得られた結果を第1表に示す。
A mixture of L-cystine and L-tyrosine is dissolved in hydrochloric acid to form a catholyte. A 5% sulfuric acid solution was used as the anolyte, and a platinum electrode was immersed in the catholyte and anolyte using a cation exchange membrane as a diaphragm, and the reduction was carried out through direct current. The catholyte is
By thin layer chromatography, shim-cystine was completely converted to L-
After confirming that it has been reduced to cysteine, aqueous ammonia is added dropwise to adjust the - value to 5, and the precipitated crystals (L-thyrodine) are collected from house to house. Further, the filtrate is oxidized by adding hydrogen peroxide solution dropwise to the nitroprusside test solution until it no longer emits blue color. Hydrochloric acid is added until the precipitated crystals are dissolved, aqueous ammonia is added dropwise to adjust the - to 2.5, and the precipitated crystals (L-cystine) are separated and recovered again. The results obtained are shown in Table 1.

7−″ 7く≦−−−−−−□−−−−−−□−−−−−−−−
−−−−−−−−−一第1表 この実験に用い′たL−シスチンは比旋光度〔α磨−2
2t、7’及ヒ含th 99.8 N (”1 ウ素滴
定法)、L−チロシ゛/は比旋光度〔α]!0−11.
6°及び含量は99.2%(マクロゲルメール法)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。
7−″ 7≦−−−−−−□−−−−−−□−−−−−−−−
−−−−−−−−−−1 Table 1 L-cystine used in this experiment has a specific optical rotation [α-2
2t, 7' and th 99.8 N ("1 urination titration method), L-tyrosine/ is the specific optical rotation [α]!0-11.
6° and a content of 99.2% (macrogelmer method) was used, and the recovery rate, optical purity, and content were all satisfactory, confirming that it is an excellent isolation method. Ta.

次に、実際にたんばく質を用いた実施例を説明する。Next, an example in which protein is actually used will be described.

実施例1 にわとりの羽毛3−に8N−塩酸6t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 6 tons of 8N hydrochloric acid is added to chicken feathers 3-, 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−5.
0に調整し、生じた沈殿をF遇する。炉取した沈殿物に
水3.5を及び塩酸ROO−を加えて溶かし、活性炭を
加えて脱色濾過する。ろ液Kかきまぜながら、アンモニ
ア水を滴下して−を4.5〜5.5に調整すると、結晶
が析出する。
The hydrolyzate was cooled and diluted with caustic soda solution (20%) for -5.
Adjust to 0 and treat the resulting precipitate with F. To the precipitate collected in the oven, 3.5 g of water and ROO- of hydrochloric acid are added to dissolve, and activated carbon is added to decolorize the precipitate by filtration. While stirring the filtrate K, aqueous ammonia is added dropwise to adjust the - to 4.5 to 5.5, and crystals are precipitated.

結晶をF遇して乾燥すると、その収量は255?であっ
た。この結晶混合物中に含まれるシスチンけ63511
i’及びチロノンは31eXであり、その他のアミノ酸
は僅少量であった。
If the crystals are dried under F treatment, the yield will be 255? Met. Cystinke 63511 contained in this crystal mixture
i' and thyronone were 31eX, and other amino acids were present in very small amounts.

この結晶混合物に3N−塩酸800−を加えて溶かして
、陰極液とする。オた陽極液は5X硫酸900−を用い
、陽イオン交換膜0.1 m’を隔膜として、陰極液中
には鉄板電極、陽極液中には炭素板電極を浸して陽イオ
ン交換膜1dm’当シ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ィによりシスチ
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、よくかきまぜながらアンモニア水を滴下し
て−を&O[調整すると結晶が析出する。
3N hydrochloric acid (800%) is added to this crystal mixture to dissolve it and prepare a catholyte. For the anolyte, 5X sulfuric acid (900%) was used, a cation exchange membrane of 0.1 m' was used as a diaphragm, an iron plate electrode was immersed in the catholyte, and a carbon plate electrode was immersed in the anolyte. Electrolytic reduction is performed through the direct current of this IA. After confirming that cystine has been completely reduced to cysteine by thin layer chromatography, the catholyte is taken out, and aqueous ammonia is added dropwise to the catholyte while stirring well, and crystals are precipitated.

この結晶を戸別(P液は保存)し、アンモニア水500
rdに溶がして活性炭を加えて濾過したν液を減圧濃縮
すること拠よシ析出した結晶を濾過して乾燥すると、七
の収量は54.61であった。
The crystals were distributed door to door (the P solution was saved), and 500% of ammonia water was added.
When the crystals precipitated were filtered and dried, the yield of 7 was 54.61.

結晶は針状で、比旋光度〔α)−’−xx、3s°、C
: 59.6%、Nニア、69%であり、L−チロシ′
ンに一致した。回収率は結晶混合物中のチロダンより換
算して69%である。
The crystal is needle-shaped and has a specific optical rotation [α)-'-xx, 3s°, C
: 59.6%, N-nia, 69%, L-tyrosi'
matched. The recovery rate is 69% based on the tyrodane in the crystal mixture.

また、前記の保存F液をよく攪拌、冷却しながら、ニト
ロプルシド試液によシ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−を加
えて溶かし、活性炭を加えて脱色濾過したろ液をよく攪
拌しながらアンモニア水を滴下して…2,5に調整する
と、結晶が析出する。析出した結晶を濾過、乾燥して得
られる収量C は157fであった。この結晶は、比旋光度〔α〕0〜
221.9°、C: 29.7%、N:11.58.%
’であり、L−シスチンに一致した。回収率は結晶混合
物中のシスチンよシ換算して97.7 Nであった。
In addition, while stirring and cooling the stored solution F well, hydrogen peroxide solution was added dropwise to the nitroprusside test solution until it no longer exhibited a blue color, and then 160-hydrochloric acid was added to the precipitated crystals to dissolve them, and activated carbon was added. Aqueous ammonia is added dropwise to the decolorized filtrate while stirring well to adjust the concentration to 2.5, and crystals are precipitated. The yield C obtained by filtering and drying the precipitated crystals was 157 f. This crystal has a specific optical rotation [α] of 0~
221.9°, C: 29.7%, N: 11.58. %
', which corresponded to L-cystine. The recovery rate was 97.7 N in terms of cystine in the crystal mixture.

実施例2 人髪3F4を用い、実施例1と同様に加水分解及び−調
整を行ない、混合結晶346vを得た。混合結晶中に含
まれるシスチンは78%、チロシンけ17,6%であっ
た。
Example 2 Human hair 3F4 was hydrolyzed and adjusted in the same manner as in Example 1 to obtain mixed crystals 346v. The mixed crystal contained 78% cystine and 17.6% tyrosine.

この混合結晶を実施例1と同様に電解還元及び結晶化を
行なうとき、L−チロジ゛ン43.2r(〔α)−−1
1,21°、C:59.62%、Nニア、71腎)を得
た。回収率は結晶混合物より換算して72にである。ま
たL−シスチンは262 F ((咲0−220、95
°、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。
When this mixed crystal is subjected to electrolytic reduction and crystallization in the same manner as in Example 1, L-tyrodine 43.2r([α)--1
1,21°, C: 59.62%, Nia, 71 kidneys) were obtained. The recovery rate is 72% calculated from the crystal mixture. In addition, L-cystine is 262 F ((Saki 0-220, 95
°, C: 29.73%, N: 11.61%). The recovery rate is 97% based on cystine in the crystal mixture.

実施例3 人髪3 Kfを用い、実施例1と同様に加水分解及び−
調整を行ない、混合結晶330vを得た。混合結晶中に
金種れるシスチンは78,6%、チロ・ツノ?i16.
9%であった。
Example 3 Human hair 3 Kf was hydrolyzed and -
After adjustment, 330v of mixed crystals were obtained. Cystine contained in mixed crystals is 78.6%, Chiro-horn? i16.
It was 9%.

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r液は別に処理)すると六、L−チhシ゛ン
4!、8F  (cαl、−11,32°1 c:59
、52%、Nニア、58N)が得られた。回収率は結晶
混合物中のチロシ′ンよシ換算し7て75πである。
This mixed crystal was subjected to electrolytic reduction and crystallization (
However, the stored r solution should be treated separately), then 6. L-chih scene 4! , 8F (cαl, -11,32°1 c:59
, 52%, N near, 58N) was obtained. The recovery rate is 75π in terms of tyrosine in the crystal mixture.

保存ν液は、窒素気流中で減圧濃縮して結晶を析出させ
、メタノールを加えて冷却し炉別する。
The stored ν liquid is concentrated under reduced pressure in a nitrogen stream to precipitate crystals, cooled by adding methanol, and separated in a furnace.

戸別し六結晶を水に溶かし、活性炭を加えて沖過し、F
液を窒素気流中で減圧濃縮して結晶を析出させる。冷後
炉別して、結晶はメタノールで洗滌したのち50Cに加
温下で減圧乾燥し、2】2vを得た。この針状結晶け)
比旋光度〔α)二〇+s、9g°、C:29.82%、
N:11.68%、ニトログルシド反応は陽性でありし
一システィンに一致した。
Dissolve the six crystals in water, add activated carbon, filter,
The liquid is concentrated under reduced pressure in a nitrogen stream to precipitate crystals. After cooling, the crystals were separated in an oven, washed with methanol, and dried under reduced pressure at 50C to obtain 2.2v. This needle-like crystal)
Specific optical rotation [α) 20+s, 9g°, C: 29.82%,
N: 11.68%, the nitroglucide reaction was positive and matched to cysteine.

またヨウ素滴定法にょシ含量は99.8 Xであった。The content determined by iodometric titration was 99.8X.

回収率は結晶混合物中のシスチンよυ換算して81.9
%である。
The recovery rate is 81.9 in terms of cystine in the crystal mixture.
%.

Claims (1)

【特許請求の範囲】[Claims] 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還元してシスティンに変換させた後
、アルカリを加えて中和し、析出するチロシンを炉別採
取し、ν液を濃縮してシスティンを析出分離するか、ま
たはF液中のシスティ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ィンおよび
チロ・ジンの単離法。
A mixture containing cystine and tyrodine is dissolved in mineral acid,
After reducing cystine in the solution and converting it to cysteine, neutralize it by adding an alkali, collect the precipitated tyrosine in a separate furnace, concentrate the ν solution and separate the cysteine, or A method for isolating cystine or cystine and tyrodine, which comprises oxidizing cystine 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 true JPS58188846A (en) 1983-11-04
JPS6012343B2 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)

Cited By (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

Cited By (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
JPS6012343B2 (en) 1985-04-01

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