JPS62187492A - Method for purifying protamine mineral acid salt - Google Patents

Method for purifying protamine mineral acid salt

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Publication number
JPS62187492A
JPS62187492A JP2974686A JP2974686A JPS62187492A JP S62187492 A JPS62187492 A JP S62187492A JP 2974686 A JP2974686 A JP 2974686A JP 2974686 A JP2974686 A JP 2974686A JP S62187492 A JPS62187492 A JP S62187492A
Authority
JP
Japan
Prior art keywords
protamine
sulfate
protamine sulfate
milt
acid salt
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
JP2974686A
Other languages
Japanese (ja)
Other versions
JPH0699477B2 (en
Inventor
Ryuzo Ueno
隆三 上野
Tatsuo Kanayama
金山 龍男
Hiroshi Kosakai
博 小堺
Katsuhiko Inui
克彦 乾
Toshio Matsuda
松田 敏生
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.)
Ueno Seiyaku Oyo Kenkyujo KK
Original Assignee
Ueno Seiyaku Oyo Kenkyujo KK
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Filing date
Publication date
Application filed by Ueno Seiyaku Oyo Kenkyujo KK filed Critical Ueno Seiyaku Oyo Kenkyujo KK
Priority to JP61029746A priority Critical patent/JPH0699477B2/en
Publication of JPS62187492A publication Critical patent/JPS62187492A/en
Publication of JPH0699477B2 publication Critical patent/JPH0699477B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To obtain the titled compound useful as an anticoagulant, etc., in high purity, simply and efficiently, by dissolving a protamine mineral acid salt obtained from milt of fish in warm water, adding a small amount of a sulfate to the warm solution in water and cooling. CONSTITUTION:Firstly, a protamine mineral acid salt is extracted from milt of fish by a well-known method, separated and dissolved in warm water usually at 40-50 deg.C. Then the warm solution in water is blended with a small amount of a sulfate, preferably 0.005-0.2mol based on 1l warm solution of the sulfate and cooled to precipitate the aimed compound. The warm solution is preferably cooled to <=5 deg.C.

Description

【発明の詳細な説明】 檄1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。[Detailed description of the invention] Fields of use on the 1st name The present invention relates to a method for purifying protamine mineral salts.

従来技術 プロタミンは分子ff1(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。
Prior art protamine has molecules ff1 (about 4000 to about 10000)
It is a relatively small basic protein that exists as a nuclear protein bound to nucleic acid (DNA) in the 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PI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 have the effect of inhibiting heparin's blood clotting, prolonging the efficacy of insulin, stabilizing enzymes, and stabilizing antibiotics, and their properties. It is used as a PI in various pharmaceutical products.

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。
Methods for purifying protamine mineral salts obtained by extraction and separation from fish milt are described, for example, in Japanese Patent Publication No. 49-24209, Japanese Patent Application Laid-Open No. 55-2612, or Japanese Patent Publication No. 59-1989.
It is disclosed in Japanese Patent No.-31519 and the like.

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. 49-24209 is a purification method in which trichloroacetic acid is added to a fish milt extract to remove impurities other than protamine as insoluble substances. This method requires operations to remove insoluble substances and to separate dissolved protamine mineral salts, and is comprised of very complicated steps. Furthermore, since the protamine mineral 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。
Furthermore, this method does not teach anything about purification using the solubility of protamine mineral salts.

特開昭55−2612号公報および特公昭59−315
19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
Japanese Unexamined Patent Publication No. 55-2612 and Japanese Patent Publication No. 59-315
The technique described in Publication No. 19 is a purification method in which an acidic dilute aqueous solution of protamine mineral salt extracted and separated from fish milt is treated with an adsorbent, and then fractionated and precipitated with an organic solvent.

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。
This method involves removing impurities other than the protamine mineral salt using an adsorbent such as activated carbon, and does not teach anything about purifying the protamine mineral salt by utilizing its solubility.

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
ろ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、無機塩の濃度か違う溶液に対して、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
4゛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
ることができろ方法を完成するに至った。
Problems to be Solved by the Invention The present inventors have investigated purification methods for obtaining protamine sulfate with higher purity and higher yield. As a result, protamine sulfate and contaminant proteins can be separated from solutions with different concentrations of inorganic salts. It was discovered that the solubility was significantly different. By utilizing this new knowledge, all of the above problems can be solved,
We have completed a method to easily and efficiently obtain highly pure protamine sulfate.

問題点を解決するための7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、次に該温水に少量の硫酸塩を
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。
Seven Steps to Solve the Problems The present invention involves dissolving protamine mineral salt obtained by extraction and separation from fish milt in hot water, then adding a small amount of sulfate to the hot water and cooling it to dissolve protamine. The present invention relates to a method for purifying protamine mineral salts, which is characterized by precipitating the mineral salts.

本発明に使用しうろ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、あるいはザバ等の白子
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 salt used in the present invention may be any protamine mineral salt obtained by extraction and separation from fish such as herring, salmon, or milt of mackerel by a known method, and is not particularly limited. It's not a thing.

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 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 hot 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 hot water may have a temperature that allows the protamine mineral salt to be 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。
Sulfates that can be used in the present invention include ammonium sulfate and sodium sulfate.

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 may be dissolved in hot water together with the protamine mineral salt, or may be added after the protamine mineral salt is added.

硫酸塩は温水1リツトルに対して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 liter of hot water. Less than 0.05 mol or 0
.. If the amount is more than 2 moles, protamine mineral salt cannot be efficiently precipitated after cooling the hot water.

温水は10℃以下、好ましくは5℃以下に冷却する。1
0℃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 hot water is cooled to below 10°C, preferably below 5°C. 1
If the temperature is higher than 0°C, 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po
2〜7の範囲にすることが望ましい。
There is no need to particularly adjust the pH of the hot water. When adjusting, add the protamine mineral salt and before adding the sulfate.
A range of 2 to 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, salts, acids, and contaminant proteins that adhere to the precipitate of protamine mineral salts when extracting and separating the milt can be removed.

本発明に従うと、魚の白子より抽出、分離した祖プロタ
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, protamine mineral salts extracted and separated from fish milt can be efficiently purified by simple means such as recrystallization.

本発明は、プロタミン鉱酸塩の溶解性が溶液lQ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〜
0.2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 is 0.05 to 0.05 to 0.05 to 0.05 to 0.05 to
This is based on the new finding that the concentration is minimized in a solution with an extremely low concentration of 0.2 mol.

表1に水温5℃、pH2,5の水溶液中における硫酸プ
ロクミンを例にとり、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lQに対して溶か
したモル数を表す。
Table 1 shows the relationship between its solubility (wt%) and sulfate concentration, taking procumin sulfate as an example in an aqueous solution with a water temperature of 5° C. and a pH of 2.5. In the table, the concentration represents the number of moles dissolved in solution lQ.

表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。
Table 1 From Table 1, the solubility of protamine sulfate is 0.05 at the salt concentration.
It can be seen that the amount becomes minimum in the range of ~0.2 mol.

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 explained in more detail using 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 milt was thawed, washed with water, drained, and ground.

摩砕した鮭の白子100gを5%(IN)硫酸500m
1に添加し、室温(24°C)で1時間攪拌した。
100g of ground salmon milt in 500ml of 5% (IN) sulfuric acid
1 and stirred at room temperature (24°C) for 1 hour.

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550m1を得た。
After stirring, the residue was removed by centrifugation to obtain 550 ml of protamine sulfate extract.

黛1 該抽出液に攪拌下、室/7+&24℃で濃アンモニア水
30m1を添加し、pHを3にコ、す整し、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。該夾惟蛋白沈澱物を遠心分離により取り除き
上澄み液630m1を得た。
Mayuzumi 1 30 ml of concentrated ammonia water was added to the extract under stirring at room temperature 7+24°C, the pH was adjusted to 3, and 124 g of ammonium sulfate was added little by little to precipitate the contaminant proteins. The accumulated protein precipitate was removed by centrifugation to obtain 630 ml of supernatant.

該上澄み液に攪拌下、室温24℃で硫酸アンモニウム1
30g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lo。
Add 11 ammonium sulfate to the supernatant at room temperature of 24°C while stirring.
30 g was gradually added to salt out protamine sulfate. The salted out protamine sulfate is separated by centrifugation to obtain white candy-like protamine sulfate.

4gを得た。4g was obtained.

置型 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100m1の温水(40〜50℃)に
溶解し、該溶液1リツトル当り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仕た。
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 DEG C.) to give an ammonium sulfate concentration of 0.09 mol per liter of the solution. Thereafter, 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 supernatant liquid of precipitated protamine sulfate was removed by decantation to obtain protamine sulfate in the form of a transparent oil. 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 process Frozen salmon milt was thawed, washed with water, drained, and ground.

摩砕した鮭の白子IKgおよび2.35モルの硫酸アン
モニウムを10%(2N)硫酸2リツトルに添加し、3
0℃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リツトルを得た。
IKg of ground salmon milt and 2.35 moles of ammonium sulfate were added to 2 liters of 10% (2N) sulfuric acid,
The mixture was stirred at 0°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。
The extract contained 53.3 g (2.13% by weight) (dry equivalent) of protamine sulfate.

分離工程 抽出液2.5リツトルを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 liters of the extract was cooled to 5° C. and allowed to stand at that temperature for 16 hours to separate the protamine sulfate precipitate and the supernatant. The supernatant liquid was collected by decantation.

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 precipitate of protamine sulfate is white and candy-like, and the yield is 102g.
Met.

回収した上澄み液は2.43リツトルであった。The amount of supernatant liquid collected was 2.43 liters.

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。
Ingredients: 7.26% sulfuric acid, 1.72 mol/liter ammonium sulfate, 1.6% by weight of protein contaminants, 0 protamine sulfate.
.. It was 4% by weight (9.72g).

精製工程 分離工程で得られた硫酸プロタミン102gを800m
1の温水(40〜50’C)に溶解し、該溶液1リツト
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 process 102g of protamine sulfate obtained in the separation process was transferred to 800m
1 of hot water (40-50'C) to give a concentration of about 0.14 mole ammonium sulfate per liter of solution. Thereafter, the solution was cooled to 5° C. and allowed to stand overnight at that temperature to separate the protamine sulfate precipitate and the supernatant liquid.

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
.2gを得た(収率4.32%)。
The supernatant liquid was removed by decantation to obtain protamine sulfate as a clear oil. It is lyophilized to produce white protamine sulfate 43.
.. 2g was obtained (yield 4.32%).

比較例1 実施例1における板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 The same procedure as in Example 1 was carried out except that the plate-making process in Example 1 was not performed. The obtained white candy-like protamine sulfate was freeze-dried to obtain 6.30 g of white protamine sulfate powder.
(yield: 6.30%).

比較例2 実施例2における肋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 The same procedure as in Example 2 was carried out except that the rib step in Example 2 was not performed. The obtained white candy-like protamine sulfate was freeze-dried to obtain 53.2 g of white protamine sulfate powder.
(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 The protamine sulfate obtained in Examples 1 and 2 and Comparative Example 1.2 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。
Purity was examined by chromatography, absorption analysis, solubility of protamine sulfate in water, and 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1:1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爪
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 chromatography. The purity of test 1:1 was compared using protamine sulfate (produced by Salmon, manufactured by Wako Pure Chemical Industries, Ltd.) as a standard, and the purity was determined as 1.00, and the purity was expressed as HPLC purity. Further, the product of the HPLC purity and the yield of the sample was shown as the standard conversion yield. Here, the standard conversion yield refers to the yield when the amount of protamine sulfate obtained from 100 g of milt is converted to protamine sulfate nails with purity equivalent to that of the standard product, and is considered to be a measure for comparing the separation efficiency of protamine sulfate. It's good. The results are shown in Table 2.

HP L C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倍ら良
いことがわかる。
A comparison of the HPLC purity shows that the purity of protamine sulfate obtained according to the present invention is about 1.2 times better than that of the comparative example.

抗菌活性は和光補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、
 5ubtilis  I AM  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。
Antibacterial activity was measured using protamine sulfate (produced by salmon) manufactured by Wako Hyakuyaku Kogyo Co., Ltd. as a standard, and Bacillus subtilis (B.
The antibacterial activity against S. 5ubtilis I AM 1069 strain was set at 1.00, and the antibacterial activity was expressed as specific activity. In addition, the product of the antibacterial activity and the sample yield was shown as the standard conversion activity yield.

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ずろと本発明に従
い得られた硫酸プC!タミンは、比較例ものよりも約1
.2倍も良いごとがわかる。
Active yield in terms of standard is the yield when converted to the amount of standard required to show the same antibacterial activity as the amount of protamine sulfate obtained from 100 g of milt. Comparison of separation efficiency of protamine sulfate It can be thought of as a measure of The results are shown in Table 2. In addition to comparing the antibacterial activity and specific activity, the sulfuric acid polypropylene C obtained according to the present invention! Tamin is about 1% higher than that of the comparative example.
.. It turns out it's twice as good.

表2 吸光分析は、核酸にに起因する260mおよび夾雑蛋白
に起因する280nmでの吸光度を測定した。
Table 2 Absorption analysis measured the absorbance at 260 nm due to nucleic acids and at 280 nm due to contaminant proteins.

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220ru++以上の光に対しては吸収がない
。表3かられ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 measurement was carried out using an aqueous solution of the sample having a concentration of 0.1% by weight at a temperature of 20°C. The results are shown in Table 3. Pure protamine sulfate has no absorption for light above 220 ru++. As can be seen from Table 3, the protamine sulfate obtained according to the present invention was compared with the protamine sulfate obtained according to the comparative example.
It can be seen that the amount of contaminant protein is extremely small.

表3 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。
Table 3 Visual observation of the solution state is a 2% aqueous solution (20°C) of each sample.
I did it. Both the protamine sulfate obtained according to the present invention and the comparative example were completely dissolved, and no insoluble matter was observed.

発明の効果 本発明に従うと魚の白子から得られた祖プロタミン鉱酸
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, protamine mineral salt obtained from fish milt can be purified without loss and through a simple process.

Claims (1)

【特許請求の範囲】[Claims] 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、次に該温水に少量の硫酸塩を添加
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。
1. Protamine mineral salt obtained by extraction and separation from fish milt is dissolved in hot water, and then a small amount of sulfate is added to the hot water and cooled to precipitate the protamine mineral salt. A 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 true JPS62187492A (en) 1987-08-15
JPH0699477B2 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)

Citations (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

Patent Citations (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
JPH0699477B2 (en) 1994-12-07

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