JPS5931519B2 - Extraction, separation and purification method of high purity protamine - Google Patents

Extraction, separation and purification method of high purity protamine

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Publication number
JPS5931519B2
JPS5931519B2 JP53074133A JP7413378A JPS5931519B2 JP S5931519 B2 JPS5931519 B2 JP S5931519B2 JP 53074133 A JP53074133 A JP 53074133A JP 7413378 A JP7413378 A JP 7413378A JP S5931519 B2 JPS5931519 B2 JP S5931519B2
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Japan
Prior art keywords
protamine
acid
extract
salt
extraction
Prior art date
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Expired
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JP53074133A
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Japanese (ja)
Other versions
JPS552613A (en
Inventor
冨郎 岩井
富保 角田
浩一 岩井
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Individual
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Individual
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  • Medicines Containing Material From Animals Or Micro-Organisms (AREA)
  • Peptides Or Proteins (AREA)

Description

【発明の詳細な説明】 本発明は、高純度プロタミンを簡易に抽出、分離、精製
する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for easily extracting, separating, and purifying high-purity protamine.

プロタミンは、サケ、マス、ニシン、サバ等の精子核中
にデオキシリボ核酸と結合したヌクレオプロタミンとし
て存在する比較的分子量の小さい高アルギニン含量の強
塩基性タンパク質である。
Protamine is a strong basic protein with a relatively small molecular weight and high arginine content, which exists as nucleoprotamine bound to deoxyribonucleic acid in the sperm nuclei of salmon, trout, herring, mackerel, etc.

プロタミンは古くより、インシュリンとの複合体である
効力持続性インシュリン製剤や抗ヘパリン剤であるプロ
タミン注射液が臨床薬剤として使用されていると同時に
、生化学研究および生化学工業において分離、精製用薬
剤としても利用されているが、近時、ある種の酵素の安
定剤や抗性物質等の活性剤あるいは助剤としても不可欠
の物質となりつゝある。従来、プロタミンの製造法とし
ては、前記魚の成熟白子を肉挽機で磨砕し、4〜5倍容
の水に懸濁させ充分攪拌した後、布または金網で濾過し
た乳状液を攪拌下に希酢酸でリトマス酸性にして、凝集
する精子核を遠心分離する。
Protamine has long been used as a clinical drug in the form of long-acting insulin preparations, which are complexes with insulin, and protamine injections, which are antiheparin agents.At the same time, protamine has been used as a drug for separation and purification in biochemical research and the biochemical industry. Recently, it has become an indispensable substance as a stabilizer for certain enzymes and as an activator or auxiliary agent for anti-inflammatory substances. Conventionally, protamine was produced by grinding the mature milt of the fish in a meat grinder, suspending it in 4 to 5 times the volume of water, stirring thoroughly, and then filtering the emulsion through a cloth or wire mesh while stirring. Make litmus acidic with dilute acetic acid and centrifuge the aggregated sperm nuclei.

さらに酢酸々性の水で洗浄を繰返し、必要に応じてアル
コールで脱脂、乾燥する。つぎにこの精子核を希鉱酸で
一定時間抽出して、残渣を遠心分離して除去し、なお残
渣の抽出を繰返す。
Furthermore, it is repeatedly washed with acetic acid water, and if necessary, it is degreased with alcohol and dried. Next, this sperm nucleus is extracted with dilute mineral acid for a certain period of time, the residue is removed by centrifugation, and the extraction of the residue is repeated.

ついで抽出液に2〜3倍容のアルコールを加えてプロタ
ミン硫酸塩として分離するか、またはピクリン酸ナトリ
ウムでプロタミン・ピタリン酸塩として沈澱させ、さら
に硫酸とアルコールでプロタミン硫酸塩として分離する
。プロタミンの精製法としての最も一般的なものは、硫
酸塩としてアルコールによる再沈澱の反覆であるが、ま
た前記のようにピクリン酸塩を経る処理が精製に効果が
あるとされて、他にも一般のタンパク沈澱剤(塩化白金
、タングステン酸、メタ燐酸、フェロシアン化水素酸、
スルホサルチル酸等)で精製し、常法により硫酸塩とす
る方法や、また近時一般的となつたイオン交換樹脂によ
る分離精製法も行なわれている。
Then, 2 to 3 times the volume of alcohol is added to the extract to separate it as protamine sulfate, or it is precipitated with sodium picrate as protamine pitalate, and further separated as protamine sulfate with sulfuric acid and alcohol. The most common purification method for protamine is repeated reprecipitation with alcohol as a sulfate salt, but as mentioned above, treatment via a picrate salt is said to be effective for purification, and there are other methods as well. General protein precipitants (platinum chloride, tungstic acid, metaphosphoric acid, ferrocyanic acid,
sulfosalcylic acid, etc.) and converting it into a sulfate salt by a conventional method, and separation and purification using an ion exchange resin, which has recently become common, are also carried out.

いずれにしても、これら従来のプロタミンの抽出、分離
、精製法は、総じて操作が煩雑で多大の労力を要するか
、または高価な機械装置あるいは資材を必要とするかし
て、大量生産には不適当であるのみか、品質の純度と収
率の相反も重なつて経済的にも著しく不利である。
In any case, these conventional protamine extraction, separation, and purification methods are generally complicated and labor-intensive, or require expensive machinery and materials, making them unsuitable for mass production. Although it is appropriate, there is also a conflict between quality purity and yield, which is extremely disadvantageous economically.

本発明者らは、前記従来法の欠点を解消する方法につい
て研究を進めた結果、高純度プロタミンを簡易に抽出、
分離、精製することができる本発明を完成するに到つた
The present inventors conducted research on methods to overcome the drawbacks of the conventional methods, and as a result, they found that they could easily extract high-purity protamine.
We have now completed the present invention, which enables separation and purification.

すなわち、本発明は、プロタミンを含有する魚の白子を
磨砕することなくそのま\の形状で直接希鉱酸で抽出し
、抽出液に縮合燐酸またはその塩を加えて難溶性のプロ
タミン塩として沈澱させ、これを高濃度無機塩類で複分
解することによりプロタミン鉱酸塩として分離し、その
酸性希薄水溶液を吸着剤で処理した後、必要最少限量ま
たはそれ以下の有機溶剤で分別沈澱させて精製すること
を特徴とする高純度プロタミンの抽出、分離、精製方法
である。本発明の特徴とする第一は、白子を磨砕するこ
となくそのま\の形状において直接希鉱酸で抽出する工
程であり、第二は、抽出液に結合燐酸あるいはその塩を
加えて難溶性のプロタミン塩として沈澱させ、これを高
濃度無機塩類で複分解することによりプロタミン鉱酸塩
を分離する工程であり、第三は、プロタミン鉱酸塩の酸
性希薄水溶液中で吸着剤で処理した後、必要最少限量の
有機溶剤で沈澱させる精製工程である。
That is, the present invention involves directly extracting protamine-containing fish milt in its original form with dilute mineral acid without grinding it, and adding condensed phosphoric acid or its salt to the extract to precipitate it as a sparingly soluble protamine salt. This is separated as protamine mineral salt by double decomposition with highly concentrated inorganic salts, and after treating the acidic dilute aqueous solution with an adsorbent, it is purified by fractional precipitation with the minimum necessary amount or less of an organic solvent. This is a method for extracting, separating, and purifying high-purity protamine. The first feature of the present invention is the process of directly extracting the milt in its original form with dilute mineral acid without grinding it, and the second is the process of adding bound phosphoric acid or its salt to the extract. This is a process in which protamine mineral salts are separated by precipitating soluble protamine salts and double decomposing them with highly concentrated inorganic salts.The third step is to separate protamine mineral salts in an acidic dilute aqueous solution of protamine mineral salts, and then treating the protamine mineral salts with an adsorbent. , is a purification process in which precipitation is performed using the minimum necessary amount of organic solvent.

以下に本発明を上記三工程に分けて詳細に説明する。一
般に動物組織よりその内容成分を調製する方法は、(1
)組織を採取する、(2)異質組織を除去する、(3)
組織を磨砕して抽出し易い状態とする。
The present invention will be explained in detail below by dividing into the above three steps. Generally, the method for preparing the contents from animal tissue is (1)
) collecting tissue, (2) removing foreign tissue, (3)
Grind the tissue to make it easier to extract.

(4)抽出に障害のある物質を水またはその他の溶剤で
洗浄して除去する、(5)目的成分を抽出する、(6)
なるべく目的成分のみを分離する、(7)目的とする純
度にまで精製する、という操作により達成される。白子
よりプロタミンの調製も上記一般法の特殊例にすぎない
。そして、プロタミン製造の従来法も極めて当然のごと
く、上記の操作に忠実に則して実行されている。すなわ
ち、すべての従来法は白子を磨砕することから出発して
いる。しかし、水に懸濁した乳状液より精子核を遠心分
離または沢過により単離する操作は困難を極める。予め
加熱するとか、有機溶剤で処理するとかいつた補助手段
を講じて高性能な遠心機をもつてしても、あるいは有効
な沢過助剤を併用するにしても、期待されるような効果
は得られない。そして、抽出後の微粒子である残滓の分
離除去も同様に多大の労力と困難を伴う。この初期の工
程における遠心分離の反覆という操作が付きまとう限り
大量生産は望むべくもなく、白子よりプロタミン調製中
における最大難点となつている。本発明の特徴とする第
一の抽出工程は、プロタミンの所在する精子核が精子頭
部にあるという白子の特殊性に着眼し、細胞核と細胞質
が緊密一体となつている一般動物組織とは異なり、物理
的な破壊により抽出し易い状態にする操作を必ずしも必
要としないということを抽出に応用したことである。
(4) Remove substances that interfere with extraction by washing with water or other solvents, (5) Extract the target component, (6)
This is achieved by separating only the target component as much as possible, and (7) refining to the target purity. The preparation of protamine from Milt is also only a special example of the above general method. As a matter of course, conventional methods for producing protamine are also carried out in accordance with the above-mentioned operations. That is, all conventional methods start from grinding the milt. However, it is extremely difficult to isolate sperm nuclei from an emulsion suspended in water by centrifugation or filtering. Even if auxiliary measures such as pre-heating or treatment with organic solvents are used, a high-performance centrifuge is used, or an effective filter aid is used, the expected effects will not be achieved. cannot be obtained. Separation and removal of the residue, which is fine particles after extraction, similarly involves a great deal of effort and difficulty. As long as repeated centrifugation steps are involved in this initial process, mass production is impossible, and this is the biggest difficulty in preparing protamine from milt. The first extraction step, which is a feature of the present invention, focuses on the uniqueness of milt in that the sperm nucleus, where protamine is located, is located in the sperm head, unlike general animal tissues, where the cell nucleus and cytoplasm are tightly integrated. This is an application of the fact that it does not necessarily require physical destruction to make it easier to extract.

すなわち白子を磨砕せずにそのま\の形で直接希鉱酸を
作用させ、酸の浸透により精子頭部よりプロタミンのみ
を溶解抽出して、しかも白子の皮膜をあたかも透析膜の
ように利用して、他の組織はほとんど白子内に残すよう
に配慮したことである。もちろん、酸に可溶な成分は同
時に抽出されるが、それは後に別の方法で除去すればよ
く、従来法の極めて微粒子の精子核や他の固形成分を物
理的に分離する労力は全く不必要となる。本発明の方法
によれば、抽出後は脱水、収縮、固化した白子がほマ無
色透明な抽出液に浮遊している状態であるので、抽出液
を流し出すことのみで完全に分離できる。希鉱酸の種類
および濃度、抽出時間および温度等の抽出条件は、常法
におけると同様自由に選択できる。
In other words, dilute mineral acid is applied directly to the milt without grinding it, and only protamine is dissolved and extracted from the sperm head through acid penetration, and the milt membrane is used as if it were a dialysis membrane. Therefore, consideration was given to leaving most of the other tissues within Shirako. Of course, the acid-soluble components are extracted at the same time, but they can be removed later by another method, completely eliminating the effort of physically separating extremely fine sperm nuclei and other solid components in conventional methods. becomes. According to the method of the present invention, after extraction, the dehydrated, shrunken, and solidified milt are suspended in a colorless and transparent extract, so they can be completely separated simply by pouring out the extract. Extraction conditions such as the type and concentration of dilute mineral acid, extraction time and temperature can be freely selected as in conventional methods.

短時間にプロタミンの完全抽出を望む場合は、酸の濃度
を高くし、常温あるいはそれ以上の温度で液の循環を実
施することが望ましい。本発明の特徴とする第二の分離
工程は、抽出液中のプロタミンを分離する方法であつて
、従来のように大量のアルコールを使用したり、あるい
はピクリン酸ナトリウム等のような特殊な沈澱剤による
ことなく、極めて一般にありふれた食品添加物としても
日常大量に使用されている縮合燐酸またはその塩を活用
して、難溶性のプロタミン塩で分離すると同時に、一部
精製効果も利用することである。縮合燐酸およびその塩
は、一般にタンパク質の沈澱剤として知られているもの
であり、プロタミンの分離精製に使用された例が米国特
許2497858にある。
If complete extraction of protamine is desired in a short period of time, it is desirable to increase the acid concentration and circulate the liquid at room temperature or higher. The second separation step, which is a feature of the present invention, is a method for separating protamine in the extract, which uses a large amount of alcohol as in the conventional method, or a special precipitant such as sodium picrate. The method is to utilize condensed phosphoric acid or its salts, which are used in large quantities on a daily basis as an extremely common food additive, to separate them using a sparingly soluble protamine salt, and at the same time to utilize a partial purification effect. . Condensed phosphoric acid and its salts are generally known as protein precipitants, and an example of their use in the separation and purification of protamine is found in US Pat. No. 2,497,858.

しかしながら、この方法が広く一般化しなかつた理由は
、プロタミンの縮合燐酸塩を通常の鉱酸塩に換える方法
に難点があつたからである。因に米国特許第24978
54においては、プロタミンメタ燐酸塩を1N硫酸に加
熱溶解して、完全に硫酸塩に変じてしまうまで煮沸する
という操作によつていることである。当然のことながら
タンパク質の加水分解の条件が伴なう結果、得られるプ
ロタミンは何らかの損傷を受けることは必定であり、こ
れがために採用をためられれたものである。本発明にお
いては、プロタミン縮合燐酸塩を高濃度無機塩類で複分
解することにより、容易にプロタミン鉱酸塩が得られる
という新知見に基づいて採用されたものである。
However, the reason why this method has not become widely popular is that there were difficulties in replacing the condensed phosphate of protamine with a normal mineral salt. Incidentally, U.S. Patent No. 24978
In No. 54, protamine metaphosphate is heated and dissolved in 1N sulfuric acid, and then boiled until it is completely converted to sulfate. Naturally, as a result of the conditions involved in protein hydrolysis, the resulting protamine is inevitably damaged in some way, and for this reason its adoption was discouraged. The present invention was adopted based on the new finding that protamine mineral salts can be easily obtained by metathesizing protamine condensed phosphates with high concentration inorganic salts.

すなわちプロタミン縮合燐酸塩は、1N硫酸ですら加熱
煮沸して始めて溶解するにもか\わらず、高濃度無機塩
類には容易に溶解してプロタミンと縮合燐酸にほと完全
に解難した状態となり、適当な塩濃度と温度変化という
単純な操作のみでプロタミン鉱酸塩を油状に分離し、分
液操作のみで単離できることである。縮合燐酸およびそ
の塩は、メタ燐酸、ポリ燐酸およびそれらの塩類いずれ
でも使用できる。また複分解用の無機塩類も鉱酸のアル
カリ塩、アルカリ土類塩、アンモニウム塩等いずれも目
的に応じて選択することができる。プロタミン縮合燐酸
塩の溶解性は無機塩濃度がほ\2モルの場合が最大であ
るが、0.5モルから飽和溶液まで液量および温度との
関連に応じて自由に選択できる。また溶解温度も塩濃度
および液量に応じて適宜に採用され、要は温度差により
プロタミンが油状に得られる条件を選べばよい。硫酸塩
を使用すればプロタミン硫酸塩が油状に分離し、アルコ
ールまたはメタノールにより脱水固化すれば硫酸プロタ
ミンの白色粉末が得られる。本発明の特徴とする第三の
精製工程は、抽出、分離したプロタミン鉱酸塩を酸性の
希薄水溶液中で吸着剤で処理した後、必要最少限量の有
機溶剤で分別沈澱させることにより、臨床薬剤としても
充分に適応できる高純度プロタミンを極めて簡易に精製
する方法である。
In other words, although protamine condensed phosphate dissolves even in 1N sulfuric acid only after heating and boiling, it easily dissolves in highly concentrated inorganic salts, leaving it in a state that is almost completely separated into protamine and condensed phosphoric acid. Protamine mineral salts can be separated into an oily state by simple operations such as appropriate salt concentration and temperature changes, and can be isolated using only liquid separation operations. As the condensed phosphoric acid and its salts, any of metaphosphoric acid, polyphosphoric acid, and salts thereof can be used. Further, inorganic salts for metathesis such as alkali salts, alkaline earth salts, and ammonium salts of mineral acids can be selected depending on the purpose. The solubility of protamine condensed phosphate is maximum when the inorganic salt concentration is about 2 mol, but it can be freely selected from 0.5 mol to a saturated solution depending on the relationship with liquid volume and temperature. Further, the dissolution temperature is appropriately selected depending on the salt concentration and the liquid amount, and the key is to select conditions that allow protamine to be obtained in the form of an oil based on the temperature difference. If a sulfate is used, protamine sulfate will separate into an oily state, and if it is dehydrated and solidified with alcohol or methanol, a white powder of protamine sulfate will be obtained. The third purification step, which is a feature of the present invention, is to treat the extracted and separated protamine mineral salt with an adsorbent in a dilute acidic aqueous solution, and then precipitate it fractionally with the minimum necessary amount of organic solvent to obtain a clinical drug. This is an extremely simple method for purifying high-purity protamine, which can be fully applied as a method for purifying protamine.

白子からの抽出液中には、プロメミン以外のタンパク質
とその分解生成物、核酸分解生成物およびある種の脂質
とその分解生成物等が混在していて、分離されたプロタ
ミン鉱酸塩にも付着してくるが、上記不純物の相対量は
原料白子、抽出条件、分離条件等により必ずしも画一的
に存在することなく、そのためにそれぞれの不純物を除
去する原理に基いて、それぞれに目標を定めて最適の除
去精製処理を実行することは実際上困難であつて、最大
公約数的な条件の下で複数の操作の巧妙な組合せを必要
とする。
The extract from Milt contains proteins other than promemin, their decomposition products, nucleic acid decomposition products, and certain lipids and their decomposition products, which also adhere to the separated protamine mineral salts. However, the relative amounts of the above impurities do not necessarily exist uniformly depending on the raw material Milt, extraction conditions, separation conditions, etc. Therefore, targets are set for each impurity based on the principle of removing each impurity. Performing optimal purification processes is difficult in practice and requires a clever combination of multiple operations under greatest common denominator conditions.

プロタミン鉱酸塩の酸性希薄水溶液中では、上記の不純
物プロタミンとの化学的結合や物理的付着は、ほとんど
切れるかまたは離れた状態で溶解していること、プロタ
ミン以外のものは吸着剤に著しい親和性のあることを利
用してほとんど除去できることを知つた。
In an acidic dilute aqueous solution of protamine mineral salt, the chemical bonds and physical adhesion with the impurity protamine mentioned above are almost completely broken or dissolved in a separated state, and substances other than protamine have a remarkable affinity for the adsorbent. I learned that most of them can be removed by using sexual characteristics.

もちろん吸着されない性質のものもあり、当然溶液中に
残存するために、沈澱操作に使用する有機溶剤の使用量
は必要最少限量であることが必要である。水溶液の濃度
は希薄であるほどよいが、1〜10%の範囲を自由に選
択できる。
Of course, some organic solvents are not adsorbed and naturally remain in the solution, so the amount of organic solvent used in the precipitation operation must be the minimum necessary amount. The concentration of the aqueous solution is preferably as dilute as possible, but it can be freely selected within the range of 1 to 10%.

酸性度は強いほど不純物の溶解性が良く、通常はPH3
以下が好ましい。一般の吸着剤(たとえば活性炭、活性
アルミナ、シリカゲル、ベントナイト、酸性白土、ケイ
ソウ土、骨炭等)はいずれも使用することができ、主と
する目的により適当に選択することができる。
The stronger the acidity, the better the solubility of impurities, usually PH3
The following are preferred. Any general adsorbent (eg, activated carbon, activated alumina, silica gel, bentonite, acid clay, diatomaceous earth, bone charcoal, etc.) can be used and can be appropriately selected depending on the main purpose.

使用量はいずれの場合も1〜10%程度でよい。温度条
件は熱時、冷時いずれでもよく、処理時間は長時間ほど
よい結果が得られる。有機溶剤もアルコール類、アセト
ン等いずれでもよく、使用量は当容以下が望ましい。以
上本発明は、(1)抽出工程、(2)分離工程、(3)
精製工程の三工程から成り、どの工程もそれぞれ従来法
と組合せてそれぞれの効果を期待できるが、特に上記の
三工程を結合した場合において最大最良の結果が得られ
る。
The amount used may be about 1 to 10% in either case. The temperature conditions may be hot or cold, and the longer the treatment time, the better results will be obtained. The organic solvent may be any alcohol, acetone, etc., and the amount used is preferably at most the equivalent volume. As described above, the present invention comprises (1) extraction step, (2) separation step, (3)
It consists of three purification steps, and each step can be combined with conventional methods to achieve its own effects, but the best results are especially obtained when the three steps mentioned above are combined.

以下、実施例をあげる。Examples are given below.

実施例 1 11月下旬に岩手県宮古で魚獲されたサケの凍結白子1
00k9を一夜放置して解凍し、0.5N塩酸250f
!を加え、常温で液の循環下に5時間抽出する。
Example 1 Frozen salmon milt caught in Miyako, Iwate Prefecture in late November 1
Let 00k9 stand overnight, thaw it, and add 250f of 0.5N hydrochloric acid.
! was added and extracted for 5 hours at room temperature while circulating the liquid.

分離した抽出液をアンモニア水でPH3〜4に調整し、
これに2.3kgのメタ燐酸ナトリウムの水溶液を攪拌
しつ\添加して一夜放置する。上澄を傾瀉してアメ状の
プロタミンメタ燐酸塩7.5kgを、151の2モル硫
酸アンモニウムに加温溶解して一夜放置する。下層の油
状プロタミン硫酸塩をアルコールで脱水固化、乾燥して
4,5kgの硫酸プロタミンの白色粉末を得る。実施例
2 実施例1と同様の方法で、ニシンの白子より得た硫酸プ
ロメミン1kgを201の水に加温溶解し、希硫酸でP
Hl.5に調整する。
The separated extract was adjusted to pH 3-4 with aqueous ammonia,
To this was added 2.3 kg of an aqueous solution of sodium metaphosphate with stirring, and the mixture was left overnight. The supernatant was decanted, and 7.5 kg of candy-like protamine metaphosphate was dissolved in 2 mol ammonium sulfate of 151 with heating and allowed to stand overnight. The lower layer of oily protamine sulfate is dehydrated and solidified with alcohol, and dried to obtain 4.5 kg of white powder of protamine sulfate. Example 2 In the same manner as in Example 1, 1 kg of promemine sulfate obtained from herring milt was dissolved under heating in 201 of water, and purified with dilute sulfuric acid.
Hl. Adjust to 5.

507の活性炭を加えて1時間攪拌後沢別する。507 activated carbon was added and stirred for 1 hour, then drained.

無色透明な硫酸プロタミン水溶液に攪拌しつ\51?の
メタノールを加え、一夜放置する。上澄液を傾瀉、アメ
状プロタミン硫酸塩を5′のメタノールで脱水固化、乾
燥する。純白色の高純度硫酸プロタミンの粉末850y
が得られる。分析結果 A.アミノ酸組成 モル%は全アミノ酸のモル数に対する各アミノ酸のモル
百分率を示す。
Stir into a colorless and transparent protamine sulfate aqueous solution\51? Add methanol and leave overnight. The supernatant liquid was decanted, and the candy-like protamine sulfate was dehydrated and solidified with 5' methanol and dried. Pure white high purity protamine sulfate powder 850y
is obtained. Analysis results A. Amino acid composition mol% indicates the mole percentage of each amino acid relative to the number of moles of all amino acids.

B.紫外部吸収B. ultraviolet absorption

Claims (1)

【特許請求の範囲】[Claims] 1 プロタミンを含有する魚の白子を磨砕することなく
そのまゝの形状で直接希鉱酸で抽出し、抽出液に縮合燐
酸またはその塩を加えて難溶性のプロタミン塩として沈
澱させ、これを高濃度無機塩類で複分解することにより
プロタミン鉱酸塩として分離し、その酸性希薄水溶液を
吸着剤で処理した後、必要最少限量の有機溶剤で分別沈
澱させて精製することを特徴とする高純度プロタミンの
抽出、分離、精製方法。
1 Extract the fish milt containing protamine directly with dilute mineral acid without grinding it, add condensed phosphoric acid or its salt to the extract, precipitate it as a sparingly soluble protamine salt, and add it to the extract. High-purity protamine is purified by separating it as protamine mineral salt by double decomposition with concentrated inorganic salts, treating the acidic dilute aqueous solution with an adsorbent, and then precipitating it fractionally with the minimum necessary amount of organic solvent. Extraction, separation and purification methods.
JP53074133A 1978-06-21 1978-06-21 Extraction, separation and purification method of high purity protamine Expired JPS5931519B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP53074133A JPS5931519B2 (en) 1978-06-21 1978-06-21 Extraction, separation and purification method of high purity protamine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP53074133A JPS5931519B2 (en) 1978-06-21 1978-06-21 Extraction, separation and purification method of high purity protamine

Publications (2)

Publication Number Publication Date
JPS552613A JPS552613A (en) 1980-01-10
JPS5931519B2 true JPS5931519B2 (en) 1984-08-02

Family

ID=13538378

Family Applications (1)

Application Number Title Priority Date Filing Date
JP53074133A Expired JPS5931519B2 (en) 1978-06-21 1978-06-21 Extraction, separation and purification method of high purity protamine

Country Status (1)

Country Link
JP (1) JPS5931519B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4954358A (en) * 1986-12-04 1990-09-04 Kabushiki Kaisha Ueno Seiyaku Oyo Kenkyujo Multiplication inhibitor for Bacillus cereus
JPH01113300A (en) * 1987-10-28 1989-05-01 Aiko:Kk Manufacturing set tool of picture and shape made of colored plastic and manufacture of picture and shape made of colored plastic by using said manufacturing set tool

Also Published As

Publication number Publication date
JPS552613A (en) 1980-01-10

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