JPH0699477B2 - Method for purifying protamine mineral acid salt - Google Patents

Method for purifying protamine mineral acid salt

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Publication number
JPH0699477B2
JPH0699477B2 JP61029746A JP2974686A JPH0699477B2 JP H0699477 B2 JPH0699477 B2 JP H0699477B2 JP 61029746 A JP61029746 A JP 61029746A JP 2974686 A JP2974686 A JP 2974686A JP H0699477 B2 JPH0699477 B2 JP H0699477B2
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Japan
Prior art keywords
protamine
sulfate
protamine sulfate
mineral acid
acid salt
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Japanese (ja)
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JPS62187492A (en
Inventor
隆三 上野
龍男 金山
博 小堺
克彦 乾
敏生 松田
Original Assignee
株式会社上野製薬応用研究所
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Description

【発明の詳細な説明】 産業上の利用分野 本発明はプロタミン鉱酸塩の精製方法に関する。TECHNICAL FIELD The present invention relates to a method for purifying protamine mineral acid salt.

従来技術 プロタミンは分子量(約4000〜約10000)の比較的小さ
い塩基性蛋白質であり、ニシン、サケ、マスなどの魚の
精子中に核酸(DNA)と結合した核蛋白として存在す
る。
2. Description of the Related Art Protamine is a relatively small basic protein having a molecular weight (about 4000 to about 10000) and exists as a nuclear protein bound to a nucleic acid (DNA) in sperm of fish such as herring, salmon and trout.

プロタミン塩類、特にその硫酸塩はヘパリンの血液凝固
を阻止する作用や、インシュリンの薬効を持続させる働
き、酵素を安定化する働きあるいは抗生物質を安定化す
る働き等が知られており、それらの性質を利用して各種
医薬品等に使用されている。
Protamine salts, especially their sulfates, are known to inhibit heparin from coagulating blood, to maintain insulin's medicinal effect, to stabilize enzymes or to stabilize antibiotics, and the like. Is used for various medicines.

魚の白子より抽出、分離して得られたプロタミン鉱酸塩
の精製方法としては、例えば特公昭49-24209号公報、特
開昭55-2612号公報あるいは特公昭59-31519号公報等に
開示されている。
As a method for purifying the protamine mineral salt obtained by extraction and separation from fish shirako, for example, it is disclosed in JP-B-49-24209, JP-A-55-2612 or JP-B-59-31519. ing.

特公昭49-24209号公報記載の技術は、魚の白子の抽出液
にトリクロル酢酸を添加してプロタミン以外の不純物を
不溶性物質として除去する精製方法である。該方法は不
溶性物質を除去する操作さらに溶解しているプロタミン
鉱酸塩を分離する操作が必要であり、非常に繁雑な工程
からなりたっている。また該方法で得られるプロタミン
鉱酸塩は純度が悪いために、さらに別の精製工程が必要
である。
The technique described in Japanese Patent Publication No. Sho 49-24209 is a purification method in which trichloroacetic acid is added to the extract of fish algae to remove impurities other than protamine as insoluble substances. This method requires an operation of removing insoluble substances and an operation of separating dissolved protamine mineral acid salt, and is a very complicated process. Further, since the protamine mineral acid salt obtained by this method has poor purity, another purification step is required.

また本方法には、プロタミン鉱酸塩の溶解度を利用して
精製することについてはなにも教示されていない。
Also, there is no teaching in the present method to utilize the solubility of protamine mineral salts for purification.

特開昭55-2612号公報および特公昭59-31519号公報に記
載の技術は、魚の白子より抽出、分離して得たプロタミ
ン鉱酸塩の酸性希薄水溶液を吸着剤で処理した後に、有
機溶剤で分別沈澱させる精製方法である。
The technology described in JP-A-55-2612 and JP-B-59-31519 is a method in which an acidic dilute aqueous solution of protamine mineral salt obtained by extraction and separation from fish shirako is treated with an adsorbent, and then an organic solvent is used. This is a purification method that separates and precipitates by.

該方法はプロタミン鉱酸塩以外の不純物を活性炭のよう
な吸着剤で除去するものであり、プロタミン鉱酸塩の溶
解度を利用して精製することについてはなにも教示され
ていない。
The method removes impurities other than protamine mineral acid with an adsorbent such as activated carbon, and teaches nothing about purification using the solubility of protamine mineral acid salt.

発明が解決しようとする問題点 本発明者らは硫酸プロタミンをより高純度、高収率で得
る精製方法を検討した結果、硫酸プロタミンおよび夾雑
蛋白は、無機塩の濃度が違う溶液に対して、溶解性を著
しく異にすることを発見した。この新たな知見を利用す
ることにより前記のような問題点をすべて解消し、純度
の高いプロタミン硫酸塩を簡便にしかも効率良く得るこ
とができる方法を完成するに至った。
Problems to be Solved by the Invention As a result of studying a purification method for obtaining protamine sulfate with higher purity and high yield, the present inventors have found that protamine sulfate and contaminant proteins are different in solutions having different inorganic salt concentrations. It was discovered that the solubilities differ markedly. By utilizing this new finding, it has been possible to solve all of the above-mentioned problems and to complete a method capable of easily and efficiently obtaining a highly pure protamine sulfate.

問題点を解決するための手段 本発明は、魚の白子より抽出、分離して得られたプロタ
ミン鉱酸塩を温水に溶解し、水に該温水1リットルに対
して0.05〜0.2モルの硫酸塩を添加し冷却することによ
りプロタミン鉱酸塩を析出させることを特徴とするプロ
タミン鉱酸塩の精製方法に関する。
MEANS FOR SOLVING THE PROBLEMS The present invention is to dissolve protamine mineral salt obtained by extracting and separating from fish spores in warm water, and adding 0.05 to 0.2 mol of sulfate to water in 1 liter of warm water. The present invention relates to a method for purifying a protamine mineral salt, which comprises depositing and cooling the protamine mineral acid salt.

本発明に使用しうるプロタミン鉱酸塩は、公知の方法に
より魚、たとえばニシン、サケ、マスあるいはサバ等の
白子から抽出、分離して得られたプロタミン鉱酸塩なら
いずれでもよく、特に限定されるものではない。
The protamine mineral acid salt that can be used in the present invention may be any protamine mineral acid salt obtained by extracting and separating from fish, for example, herring, salmon, trout or mackerel, etc., by a known method, and is not particularly limited. Not something.

本発明においてはプロタミン鉱酸塩として硫酸プロタミ
ンを使用することが好ましい。
In the present invention, it is preferable to use protamine sulfate as the protamine mineral acid salt.

温水に溶かすプロタミン鉱酸塩の濃度は濃厚な程良い。The higher the concentration of protamine mineral salt dissolved in warm water, the better.

温水は、溶解させるプロタミン鉱酸塩が溶解する温度で
あればよい。
The warm water may be at a temperature at which the protamine mineral salt to be dissolved is dissolved.

本発明に使用できる硫酸塩は硫酸アンモニウムあるいは
硫酸ナトリウム等である。
The sulfate that can be used in the present invention is ammonium sulfate, sodium sulfate or the like.

硫酸塩はプロタミン鉱酸塩とともに温水に溶解してもよ
いし、プロタミン鉱酸塩を添加した後に添加してもよ
い。
The sulfate salt may be dissolved in warm water together with the protamine mineral acid salt, or may be added after adding the protamine mineral acid salt.

硫酸塩は温水1リットルに対して0.05〜0.2モルの量を
添加する。0.05モルより少ないかあるいは0.2モルより
多いと温水を冷却後プロタミン鉱酸塩を効率良く析出さ
せることができない。
Sulfate is added in an amount of 0.05 to 0.2 mol per 1 liter of warm water. If it is less than 0.05 mol or more than 0.2 mol, the protamine mineral acid salt cannot be efficiently precipitated after cooling the warm water.

温水は10℃以下、好ましくは5℃以下に冷却する。10℃
より高いとプロタミン鉱酸塩を効率良く析出させること
ができない。
The warm water is cooled to 10 ° C or lower, preferably 5 ° C or lower. 10 ° C
If it is higher, the protamine mineral salt cannot be efficiently precipitated.

温水のpHは特に調整する必要はない。調整する場合は、
プロタミン鉱酸塩を添加後硫酸塩を添加する前にpH2〜
7の範囲にすることが望ましい。
It is not necessary to adjust the pH of hot water. When adjusting,
After adding protamine minerals and before adding sulfate
A range of 7 is desirable.

本発明に従い精製を行うことにより、白子を抽出、分離
する際プロタミン鉱酸塩の析出物に付着する塩、酸およ
び夾雑蛋白を除去できる。
By performing purification according to the present invention, it is possible to remove salts, acids and contaminating proteins adhering to the precipitate of protamine mineral acid salt during extraction and separation of Miko.

本発明に従うと、魚の白子より抽出、分離した粗プロタ
ミン鉱酸塩を再結晶のごとき簡単な手段でかつ効率よく
精製することができる。
According to the present invention, the crude protamine mineral salt extracted and separated from the white larva of fish can be efficiently purified by a simple means such as recrystallization.

本発明は、プロタミン鉱酸塩の溶解性が溶液1に対し
て硫酸アンモニウムあるいは硫酸ナトリウム0.05〜0.6
モル溶けた極めて低い濃度域の溶液中で最小になるとい
う新たな知見に基づくものである。
In the present invention, the solubility of protamine mineral salt in solution 1 is 0.05 to 0.6 of ammonium sulfate or sodium sulfate.
It is based on the new finding that it is minimized in a solution in a very low concentration range which is dissolved in a molar state.

表1に水温5℃、pH2.5の水溶液中における硫酸プロタ
ミンを例にとり、その溶解度(重量%)と硫酸塩濃度の
関係を表した。表中、濃度は溶液1に対して溶かした
モル数を表す。
Table 1 shows the relationship between the solubility (% by weight) and the sulfate concentration of protamine sulfate in an aqueous solution having a water temperature of 5 ° C. and pH 2.5. In the table, the concentration represents the number of moles dissolved in Solution 1.

表1より硫酸プロタミンの溶解度は塩の濃度が0.05〜0.
2モルの範囲で最小になるのがわかる。
From Table 1, the solubility of protamine sulphate is such that the salt concentration is 0.05 to 0.
It can be seen that it becomes the minimum in the range of 2 moles.

本発明を実施例を用いてさらに詳しく説明する。The present invention will be described in more detail with reference to examples.

実施例1 抽出 冷凍した鮭の白子を解凍、水洗い、水切りを行い摩砕し
た。
Example 1 Extraction Frozen salmon shirako was thawed, washed with water, drained and ground.

摩砕した鮭の白子100gを5%(1N)硫酸500mlに添加
し、室温(24℃)で1時間攪拌した。攪拌後、残渣を遠
心分離により取り除き硫酸プロタミン抽出液550mlを得
た。
100 g of ground salmon Shirako was added to 500 ml of 5% (1N) sulfuric acid, and the mixture was stirred at room temperature (24 ° C) for 1 hour. After stirring, the residue was removed by centrifugation to obtain 550 ml of protamine sulfate extract.

分離 該抽出液に攪拌下、室温24℃で濃アンモニア水30mlを添
加し、pHを3に調整し、さらに硫酸アンモニウム124gを
少量ずつ添加し、夾雑蛋白を沈澱させた。該夾雑蛋白沈
澱物を遠心分離により取り除き上澄み液630mlを得た。
Separation To the extract, 30 ml of concentrated ammonia water was added at room temperature of 24 ° C. with stirring to adjust the pH to 3, and 124 g of ammonium sulfate was added little by little to precipitate contaminating proteins. The contaminant protein precipitate was removed by centrifugation to obtain 630 ml of a supernatant.

該上澄み液に攪拌下、室温24℃で硫酸アンモニア130gを
徐々に添加し硫酸プロタミンを塩析させた。塩析した硫
酸プロタミンを遠心分離により分離し、白色飴状の硫酸
プロタミン10.4gを得た。
While stirring, 130 g of ammonium sulfate was gradually added to the supernatant at room temperature of 24 ° C. to salt out protamine sulfate. The salted-out protamine sulfate was separated by centrifugation to obtain 10.4 g of white candy-like protamine sulfate.

精製 さらに以上のようにして得られた白色飴状の硫酸プロタ
ミン10.4gを100mlの温水(40〜50℃)に溶解し、該溶液
1リットル当り0.09モルの硫酸アンモニウムの濃度とし
た。その後溶液を5℃に冷却しその温度で2日間放置し
硫酸プロタミンを析出させた。
Purification Further, 10.4 g of white candy-like protamine sulfate obtained as described above was dissolved in 100 ml of warm water (40 to 50 ° C.), and the concentration of ammonium sulfate was 0.09 mol per liter of the solution. Then, the solution was cooled to 5 ° C. and left at that temperature for 2 days to precipitate protamine sulfate.

析出した硫酸プロタミンの上澄み液を傾瀉して取り除
き、透明油状の硫酸プロタミンを得た。それを凍結乾燥
し白色の硫酸プロタミン4.76gを得た(収率4.76%)。
The precipitated supernatant of protamine sulfate was decanted off to obtain a transparent oily protamine sulfate. It was freeze-dried to obtain 4.76 g of white protamine sulfate (yield 4.76%).

実施例2 抽出工程 冷凍した鮭の白子を解凍、水洗い、水切りを行い摩砕し
た。
Example 2 Extraction Step Frozen salmon Shiroko was thawed, washed with water, drained and ground.

摩砕した鮭の白子1Kgおよび2.35モルの硫酸アンモニウ
ムを10%(2N)硫酸2lに添加し、30℃1時間攪拌した。
攪拌後、残渣を遠心分離により取り除き硫酸プロタミン
抽出液2.5リットルを得た。
1 kg of ground salmon Shirako and 2.35 mol of ammonium sulfate were added to 2 l of 10% (2N) sulfuric acid and stirred at 30 ° C for 1 hour.
After stirring, the residue was removed by centrifugation to obtain 2.5 liters of protamine sulfate extract.

抽出液中には硫酸プロタミンが53.3g(2.13重量%)
(乾燥換算)含まれていた。
53.3 g (2.13% by weight) of protamine sulfate in the extract
It was included (dry conversion).

分離工程 抽出液2.5lを5℃に冷却しその温度で16時間静置し、硫
酸プロタミン析出物と上澄み液とに分離させた。上澄み
液は傾瀉して回収した。
Separation step 2.5 l of the extract was cooled to 5 ° C. and allowed to stand at that temperature for 16 hours to separate a protamine sulfate precipitate and a supernatant. The supernatant was decanted and collected.

硫酸プロタミン析出物は白色アメ状で、収量は102gであ
った。
The protamine sulfate precipitate was white candy-like, and the yield was 102 g.

回収した上澄み液は2.43リットルであった。成分は硫酸
7.26%、硫酸アンモニウム1.72モル/リットル、夾雑蛋
白1.6重量%、硫酸プロタミン0.4重量%(9.72g)であ
った。
The recovered supernatant was 2.43 liters. Component is sulfuric acid
The content was 7.26%, ammonium sulfate 1.72 mol / liter, contaminating protein 1.6% by weight, and protamine sulfate 0.4% by weight (9.72 g).

精製工程 分離工程で得られた硫酸プロタミン102gを800mlの温水
(40〜50℃)に溶解し、該溶液1リットル当たり約0.14
モルの硫酸アンモニウムの濃度とした。その後溶液を5
℃に冷却しその温度で一夜静置し硫酸プロタミン析出物
と上澄み液とに分離させた。
Purification step 102 g of protamine sulfate obtained in the separation step was dissolved in 800 ml of warm water (40 to 50 ° C), and about 0.14 per liter of the solution was dissolved.
The concentration was molar ammonium sulfate. Then add the solution to 5
The mixture was cooled to 0 ° C. and allowed to stand overnight at that temperature to separate a protamine sulfate precipitate and a supernatant.

上澄み液を傾瀉して取り除き、透明油状の硫酸プロタミ
ンを得た。それを凍結乾燥し白色の硫酸プロタミン43.2
gを得た(収率4.32%)。
The supernatant liquid was decanted and removed to obtain a transparent oily protamine sulfate. Lyophilize it and white Protamine Sulfate 43.2
g was obtained (yield 4.32%).

比較例1 実施例1における精製工程を行わない以外は実施例1と
同様におこなった。得られた白色飴状の硫酸プロタミン
を凍結乾燥し、白色の硫酸プロタミンの粉末6.30g(収
率6.30%)を得た。
Comparative Example 1 Example 1 was repeated except that the purification step in Example 1 was not performed. The obtained white candy-like protamine sulfate was lyophilized to obtain 6.30 g (yield 6.30%) of white protamine sulfate powder.

比較例2 実施例2における精製工程を行なわない以外は実施例2
と同様におこなった。得られた白色飴状の硫酸プロタミ
ンを凍結乾燥し、白色の硫酸プロタミンの粉末53.2g
(収率5.32%)を得た。
Comparative Example 2 Example 2 except that the purification step in Example 2 was not performed.
Same as above. The obtained white candy-like protamine sulfate was freeze-dried, and 53.2 g of white protamine sulfate powder was obtained.
(Yield 5.32%) was obtained.

実施例3 実施例1、2および比較例1、2で得た硫酸プロタミン
を試料とし、その純度を測定した。
Example 3 Protamine sulfate obtained in Examples 1 and 2 and Comparative Examples 1 and 2 was used as a sample, and its purity was measured.

純度はクロマトグラフィー、吸光分析、硫酸プロタミン
を水に溶かした時の溶液の溶状および抗菌活性により検
討した。
The purity was examined by chromatography, absorption spectrometry, the solubility of the solution when protamine sulfate was dissolved in water, and the antibacterial activity.

クロマトグラフィーは高速液体クロマトグラフィーを使
用した。試料の純度は和光純薬工業製硫酸プロタミン
(鮭製)を標品とし、その純度を1.00として比較しHPLC
純度として示した。またHPLC純度と試料の収率を掛けた
ものを標品換算収率として示した。ここで標品換算収率
とは白子100gから得られる硫酸プロタミンの量を標品程
度の純度を有した硫酸プロタミン量に換算した場合の収
率を言い、硫酸プロタミンの分離効率比較の尺度と考え
て良い。それらの結果を表2中に示した。
High performance liquid chromatography was used for the chromatography. The purity of the sample was determined by using Wako Pure Chemical Industries, Ltd. Protamine Sulfate (salmon) as the standard, and comparing it with the purity of 1.00.
Shown as purity. In addition, the product obtained by multiplying the HPLC purity by the sample yield is shown as the standard product yield. Here, the standardized yield refers to the yield when the amount of protamine sulfate obtained from 100 g of white roe is converted to the amount of protamine sulfate having a purity of about the standard, and is considered as a scale for comparison of separation efficiency of protamine sulfate. Good. The results are shown in Table 2.

HLPC純度を比較すると、本発明に従い得られた硫酸プロ
タミンの純度は、比較例に比べ約1.2倍も良いことがわ
かる。
Comparing the HLPC purities, it can be seen that the purity of protamine sulfate obtained according to the present invention is about 1.2 times better than that of the comparative example.

抗菌活性は和光純薬工業製硫酸プロタミン(鮭製)を標
品に使用し、ペーパーディスク法において枯草菌(B.su
btilis IAM 1069株)に対する抗菌活性を1.00として比
較し抗菌力比活性として示した。また抗菌力比活性と試
料の収率を掛けたものを標品換算活性収率として示し
た。標品換算活性収率とは白子100gから得られる硫酸プ
ロタミンの量に対して同等の抗菌力を示すために必要と
する標品の量に換算した場合の収率を言い硫酸プロタミ
ンの分離効率比較の尺度と考えて良い。それらの結果を
表2中に示した。抗菌力比活性を比較すると本発明に従
い得られた硫酸プロタミンは、比較例のものよりも約1.
2倍も良いことがわかる。
For antibacterial activity, protamine sulfate (salmon) manufactured by Wako Pure Chemical Industries, Ltd. was used as a standard, and B. subtilis ( B.su
The antibacterial activity against btilis IAM 1069 strain) was compared as 1.00 and shown as the antibacterial activity specific activity. In addition, the product obtained by multiplying the specific activity of antibacterial activity and the yield of the sample is shown as the standardized active yield. The standardized active yield refers to the yield when converted to the amount of the standard required to show the same antibacterial activity as the amount of protamine sulfate obtained from 100 g of Shiroko.Comparison of separation efficiency of protamine sulfate You can think of it as a measure of. The results are shown in Table 2. When comparing the antibacterial activity specific activity, protamine sulfate obtained according to the present invention is about 1.
You can see that it is twice as good.

吸光分析は、核酸に起因する260nmおよび夾雑蛋白質に
起因する280nmでの吸光度を測定した。測定は試料の濃
度0.1重量%の水溶液を温度20℃で行なった。その結果
を表3中に示した。純粋な硫酸プロタミンは220nm以上
の光に対しては吸収がない。表3からわかるように本発
明に従い得られた硫酸プロタミンは比較例により得られ
た硫酸プロタミンに比べ、夾雑蛋白の量が非常に少ない
ことがわかる。
The absorption spectrometry measured the absorbance at 260 nm attributed to nucleic acid and 280 nm attributed to contaminant protein. The measurement was carried out at a temperature of 20 ° C. in an aqueous solution containing 0.1% by weight of the sample. The results are shown in Table 3. Pure protamine sulfate does not absorb light above 220 nm. As can be seen from Table 3, the protamine sulfate obtained according to the present invention has a much smaller amount of contaminating proteins than the protamine sulfate obtained according to the comparative example.

溶液状態の目視観察は、各試料の2%水溶液(20℃)で
行なった。本発明および比較例に従い得られた硫酸プロ
タミンともに完全に溶解し、不溶物の存在が認められな
かった。
The visual observation of the solution state was performed with a 2% aqueous solution (20 ° C.) of each sample. Both protamine sulfate obtained according to the present invention and the comparative example were completely dissolved, and the presence of insoluble matter was not recognized.

発明の効果 本発明に従うと魚の白子から得られた粗プロタミン鉱酸
塩を損失なく、しかも簡便な工程で、精製することがで
きる。
EFFECTS OF THE INVENTION According to the present invention, crude protamine mineral acid salt obtained from fish spores can be purified by a simple process without loss.

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特公 昭49−24209(JP,B1) 特公 昭59−31518(JP,B2) ─────────────────────────────────────────────────── ─── Continuation of the front page (56) References Japanese Patent Publication Sho 49-24209 (JP, B1) Japanese Patent Publication Sho 59-31518 (JP, B2)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】魚の白子より抽出、分離して得られたプロ
タミン鉱酸塩を温水に溶解し、次に該温水1リットルに
対して0.05〜0.2モルの硫酸塩を添加し冷却することを
特徴とするプロタミン鉱酸塩の精製方法。
1. A protamine mineral acid salt obtained by extraction and separation from fish shirako is dissolved in warm water, and then 0.05 to 0.2 mol of a sulfate salt is added to 1 liter of the warm water, followed by cooling. Method for purifying protamine mineral salt.
JP61029746A 1986-02-12 1986-02-12 Method for purifying protamine mineral acid salt Expired - Fee Related JPH0699477B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61029746A JPH0699477B2 (en) 1986-02-12 1986-02-12 Method for purifying protamine mineral acid salt

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61029746A JPH0699477B2 (en) 1986-02-12 1986-02-12 Method for purifying protamine mineral acid salt

Publications (2)

Publication Number Publication Date
JPS62187492A JPS62187492A (en) 1987-08-15
JPH0699477B2 true JPH0699477B2 (en) 1994-12-07

Family

ID=12284661

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61029746A Expired - Fee Related JPH0699477B2 (en) 1986-02-12 1986-02-12 Method for purifying protamine mineral acid salt

Country Status (1)

Country Link
JP (1) JPH0699477B2 (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4924209A (en) * 1972-06-30 1974-03-04
JPS5931518A (en) * 1982-08-17 1984-02-20 三菱電機株式会社 Method of mounting part

Also Published As

Publication number Publication date
JPS62187492A (en) 1987-08-15

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