JPS6215196B2 - - Google Patents
Info
- Publication number
- JPS6215196B2 JPS6215196B2 JP16579878A JP16579878A JPS6215196B2 JP S6215196 B2 JPS6215196 B2 JP S6215196B2 JP 16579878 A JP16579878 A JP 16579878A JP 16579878 A JP16579878 A JP 16579878A JP S6215196 B2 JPS6215196 B2 JP S6215196B2
- Authority
- JP
- Japan
- Prior art keywords
- urokinase
- ion
- polysaccharide granules
- crude
- solution
- 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
Links
- 102000003990 Urokinase-type plasminogen activator Human genes 0.000 claims description 29
- 108090000435 Urokinase-type plasminogen activator Proteins 0.000 claims description 29
- 229960005356 urokinase Drugs 0.000 claims description 29
- 150000004676 glycans Chemical class 0.000 claims description 13
- 239000008187 granular material Substances 0.000 claims description 13
- 229920001282 polysaccharide Polymers 0.000 claims description 13
- 239000005017 polysaccharide Substances 0.000 claims description 13
- 239000007853 buffer solution Substances 0.000 claims description 8
- 239000000243 solution Substances 0.000 claims description 5
- 102100039419 Plasminogen activator inhibitor 2 Human genes 0.000 claims description 4
- 239000002797 plasminogen activator inhibitor Substances 0.000 claims description 4
- 108010065822 urokinase inhibitor Proteins 0.000 claims description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- 238000010828 elution Methods 0.000 claims description 2
- 238000011084 recovery Methods 0.000 claims 1
- 239000000126 substance Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 8
- 238000005342 ion exchange Methods 0.000 description 7
- 238000000746 purification Methods 0.000 description 7
- 238000001042 affinity chromatography Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 239000012535 impurity Substances 0.000 description 5
- 102000004190 Enzymes Human genes 0.000 description 4
- 108090000790 Enzymes Proteins 0.000 description 4
- 229940088598 enzyme Drugs 0.000 description 4
- 230000001698 pyrogenic effect Effects 0.000 description 4
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 3
- 239000000872 buffer Substances 0.000 description 3
- 239000002510 pyrogen Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 235000002639 sodium chloride Nutrition 0.000 description 3
- 238000005349 anion exchange Methods 0.000 description 2
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 229920002678 cellulose Polymers 0.000 description 2
- 239000012266 salt solution Substances 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 210000002700 urine Anatomy 0.000 description 2
- 229920000936 Agarose Polymers 0.000 description 1
- QYPPJABKJHAVHS-UHFFFAOYSA-N Agmatine Natural products NCCCCNC(N)=N QYPPJABKJHAVHS-UHFFFAOYSA-N 0.000 description 1
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 1
- 229920002307 Dextran Polymers 0.000 description 1
- 239000001856 Ethyl cellulose Substances 0.000 description 1
- ZZSNKZQZMQGXPY-UHFFFAOYSA-N Ethyl cellulose Chemical compound CCOCC1OC(OC)C(OCC)C(OCC)C1OC1C(O)C(O)C(OC)C(CO)O1 ZZSNKZQZMQGXPY-UHFFFAOYSA-N 0.000 description 1
- CHJJGSNFBQVOTG-UHFFFAOYSA-N N-methyl-guanidine Natural products CNC(N)=N CHJJGSNFBQVOTG-UHFFFAOYSA-N 0.000 description 1
- 208000007536 Thrombosis Diseases 0.000 description 1
- 239000008351 acetate buffer Substances 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- QYPPJABKJHAVHS-UHFFFAOYSA-P agmatinium(2+) Chemical compound NC(=[NH2+])NCCCC[NH3+] QYPPJABKJHAVHS-UHFFFAOYSA-P 0.000 description 1
- -1 aminobutylene guanidine Chemical compound 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- ZRALSGWEFCBTJO-UHFFFAOYSA-N anhydrous guanidine Natural products NC(N)=N ZRALSGWEFCBTJO-UHFFFAOYSA-N 0.000 description 1
- 239000002246 antineoplastic agent Substances 0.000 description 1
- 229940041181 antineoplastic drug Drugs 0.000 description 1
- 239000008366 buffered solution Substances 0.000 description 1
- 239000001768 carboxy methyl cellulose Substances 0.000 description 1
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 1
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 1
- 238000005341 cation exchange Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000000502 dialysis Methods 0.000 description 1
- SWSQBOPZIKWTGO-UHFFFAOYSA-N dimethylaminoamidine Natural products CN(C)C(N)=N SWSQBOPZIKWTGO-UHFFFAOYSA-N 0.000 description 1
- 229920001249 ethyl cellulose Polymers 0.000 description 1
- 235000019325 ethyl cellulose Nutrition 0.000 description 1
- 238000002523 gelfiltration Methods 0.000 description 1
- 238000004255 ion exchange chromatography Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 208000010125 myocardial infarction Diseases 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000008055 phosphate buffer solution Substances 0.000 description 1
- 229940080469 phosphocellulose Drugs 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 1
Landscapes
- Enzymes And Modification Thereof (AREA)
Description
本発明はウロキナーゼの精製法に関する。その
目的は活性が高くしかも発熱性物質を含まないウ
ロキナーゼを得ることにある。
ウロキナーゼは人尿中に存在する酵素であり、
末梢動静脈血栓症および心筋硬塞症の治療に有用
な物質である。このウロキナーゼはゲル過、イ
オン交換クロマトグラフイー、アフイニテイクロ
マトグラフイー等の手段により得られるが、これ
らの方法によると不純物特に発熱性物質および活
性のない物質の除去が完全でないために単位当り
の活性の高いものが得られなかつた。また、この
分離操作も複雑でありそして操作に用いた装置も
反復使用がむつかしい等の欠点を有していた。
本発明者は前記欠点を解決すべく研究を行つた
結果、粗製ウロキナーゼを精製する際に粗製ウロ
キナーゼをイオン交換多糖体顆粒に接触させた後
アフイニテイークロマトグラフイーを行うことに
より、単位当りの活性が極めて高く、かつ発熱性
物質をほとんど含まないウロキナーゼが収率よく
得られることを見出して本発明を完成するに至つ
た。
本発明は、粗製ウロキナーゼの緩衝溶液をイオ
ン交換多糖体顆粒に接触させて得られた溶液を合
成ウロキナーゼ阻害剤を炭素鎖を介して多糖体顆
粒と結合せしめてなる担体と接触させ、ウロキナ
ーゼを吸着させた後、溶離させるウロキナーゼの
精製法である。
本発明で云う「粗製ウロキナーゼ」とは例えば
硫酸バリウム、珪酸およびその塩類、ならびに各
種イオン交換体等の吸着剤または硫安等の沈澱済
を用いて人尿より分離した段階のウロキナーゼを
云う。
また「イオン交換多糖体顆粒」とは、セルロー
ス、交叉結合デキストラン、アガロース等の多糖
体顆粒にイオン交換基を結合せしめたものを云
い、例としてジエチルアミノエチルセフアデツク
ス(フマルマシア社製)、ジエチルアミノエチル
セルロース、トリエチルアミノエチルセルロー
ス、アミノエチルセルロース、グアニドエチルセ
ルロース等の陰イオン交換多糖体顆粒、カルボキ
シメチルセフアデツクス、スルホニルエチルセフ
アデツクス(以上フアルマシア社製)、カルボキ
シメチルセルロース、ホスホセルロース、ホスホ
ノメチルセルロース、スルホノエチルセルロー
ス、スルホノメチルセルロース等の陽イオン交換
多糖体顆粒が挙げられる。
さらにまた「合成ウロキナーゼ阻害剤」とはウ
ロキナーゼの作用を特異的に阻害する物質で例え
ばパラアミノベンズアミジン、メタアミノベンズ
アミジン、アグマチン(アミノブチレングアニジ
ン)等の物質が挙げられる。この合成ウロキナー
ゼ阻害剤と前記したような多糖体顆粒とを炭素鎖
スペーサーを介して結合せしめた担体をアフイニ
テイークロマトグラフイーに用いる。この担体は
例えば「Biochimica et Biophysica Acta」第445
巻第215〜222頁(1976)に記載の方法により容易
に製造することができる。
本発明の方法はまず粗製ウロキナーゼの緩衝溶
液をイオン交換多糖体顆粒に接触させる。この場
合に用いる緩衝液の種類および濃度は、イオン交
換多糖体顆粒の種類および酵素の状態により異る
が、例えば陰イオン交換多糖体顆粒を用いた場合
はPH6〜8程度の塩基性緩衝液等が用いられ、緩
衝液の濃度は0.05〜0.3モルが適当である。精製
の対象となる粗製ウロキナーゼが特に多くの不純
物を含む場合は前記に示した緩衝液の濃度範囲の
うちの高い部分、すなわち0.1〜0.3モルの濃度を
用いるとよい。しかし緩衝液の濃度が前記範囲を
越えるとこの精製の主たる目的である発熱性物質
の除去が行われないために好ましくない。イオン
交換精製時の他の条件、例えば粗製ウロキナーゼ
の緩衝溶液の流速等は各々の場合に応じて適宜選
択されうる。
前記イオン交換精製処理を行つて得られたウロ
キナーゼ溶液は粗製ウロキナーゼに含まれる発熱
性物質の殆どが除去されたものであり、これを次
にアフイニテイー用担体と接触させ更に精製を行
う。
まずウロキナーゼ溶液をアフイニテイクロマト
グラフイーの条件に適した緩衝液に透析等の方法
で置換する。この時の緩衝液はアフイニテイクロ
マトグラフイーの種類そして酵素溶液の状態に適
したものが用いられ、食塩を含むりん酸緩衝液等
の中性の高濃度塩類溶液が例として挙げられる。
前記のように調整されたウロキナーゼ緩衝溶液
はアフイニテイ用担体と接触させる。この処理に
よりウロキナーゼは担体に吸着され、他の主とし
て蛋白質である不純物はクロマトグラフ系外に流
出し、ウロキナーゼと不純物との分離を行うこと
ができる。担体に吸着しているウロキナーゼは、
例えば食塩を含む酢酸緩衝液等の低PH高濃度塩類
溶液を通過せしめることによりカラムより流出す
る。
このようにして得られたウロキナーゼは不純物
特に発熱性物質および不活性物質を含まないため
単位当りの活性が非常に高く、制癌剤と併用する
場合に特に有用である。
また操作工程も簡易であるために精製中の活性
の低下、収率の低下、酵素の分解等もみられず非
常に優れた方法である。
本発明の方法によれば以下のような分離過程を
経て極めて効果的なウロキナーゼの精製が実現さ
れるものと推定される。
The present invention relates to a method for purifying urokinase. The aim is to obtain urokinase with high activity and no pyrogenic substances. Urokinase is an enzyme present in human urine.
It is a useful substance in the treatment of peripheral arteriovenous thrombosis and myocardial infarction. This urokinase can be obtained by gel filtration, ion exchange chromatography, affinity chromatography, etc., but these methods do not completely remove impurities, especially pyrogens and inactive substances, so the amount per unit is low. A product with high activity could not be obtained. Moreover, this separation operation is also complicated, and the equipment used for the operation has drawbacks such as difficulty in repeated use. As a result of research to solve the above-mentioned drawbacks, the present inventor has found that when purifying crude urokinase, the activity per unit can be improved by bringing the crude urokinase into contact with ion-exchange polysaccharide granules and then performing affinity chromatography. The present inventors have completed the present invention by discovering that urokinase, which has extremely high pyrogenicity and contains almost no pyrogenic substances, can be obtained in good yield. In the present invention, a solution obtained by contacting a buffer solution of crude urokinase with ion-exchanged polysaccharide granules is contacted with a carrier made of a synthetic urokinase inhibitor bound to polysaccharide granules via carbon chains, and urokinase is adsorbed. This is a purification method for urokinase in which the urokinase is purified by elution. The term "crude urokinase" as used in the present invention refers to urokinase separated from human urine using adsorbents such as barium sulfate, silicic acid and its salts, various ion exchangers, or precipitated substances such as ammonium sulfate. In addition, "ion-exchange polysaccharide granules" refer to polysaccharide granules such as cellulose, cross-linked dextran, agarose, etc., with ion-exchange groups bonded to them. , anion exchange polysaccharide granules such as triethylaminoethylcellulose, aminoethylcellulose, guanidoethylcellulose, carboxymethylcephadex, sulfonylethylscephadex (manufactured by Pharmacia), carboxymethylcellulose, phosphocellulose, phosphonomethylcellulose, sulfonate Examples include cation exchange polysaccharide granules such as ethyl cellulose and sulfonomethyl cellulose. Furthermore, the term "synthetic urokinase inhibitor" refers to a substance that specifically inhibits the action of urokinase, and includes, for example, para-aminobenzamidine, meta-aminobenzamidine, agmatine (aminobutylene guanidine), and the like. A carrier in which this synthetic urokinase inhibitor and polysaccharide granules as described above are bound via a carbon chain spacer is used for affinity chromatography. This carrier can be used, for example, in "Biochimica et Biophysica Acta" No. 445.
It can be easily produced by the method described in Vol. 215-222 (1976). In the method of the present invention, first, a buffered solution of crude urokinase is brought into contact with ion exchange polysaccharide granules. The type and concentration of the buffer used in this case varies depending on the type of ion exchange polysaccharide granules and the state of the enzyme, but for example, when using anion exchange polysaccharide granules, a basic buffer with a pH of about 6 to 8, etc. is used, and the appropriate concentration of the buffer is 0.05 to 0.3 mol. If the crude urokinase to be purified contains a particularly large number of impurities, it is preferable to use a buffer solution in the higher range of the concentration range shown above, that is, a concentration of 0.1 to 0.3 molar. However, if the concentration of the buffer solution exceeds the above range, the removal of pyrogenic substances, which is the main purpose of this purification, will not be achieved, which is undesirable. Other conditions during ion-exchange purification, such as the flow rate of a buffer solution of crude urokinase, can be appropriately selected depending on each case. The urokinase solution obtained by the ion exchange purification treatment is one in which most of the pyrogenic substances contained in the crude urokinase have been removed, and is then brought into contact with an affinity carrier for further purification. First, the urokinase solution is replaced with a buffer solution suitable for the conditions of affinity chromatography by a method such as dialysis. At this time, a buffer solution suitable for the type of affinity chromatography and the state of the enzyme solution is used, such as a neutral high concentration salt solution such as a phosphate buffer solution containing common salt. The urokinase buffer solution prepared as described above is brought into contact with the affinity carrier. Through this treatment, urokinase is adsorbed onto the carrier, and other impurities, mainly proteins, flow out of the chromatographic system, allowing separation of urokinase and impurities. Urokinase adsorbed on the carrier is
For example, it flows out from the column by passing a low-PH, high-concentration salt solution such as an acetate buffer containing sodium chloride. Since the urokinase thus obtained does not contain impurities, particularly pyrogens and inert substances, it has very high activity per unit, and is particularly useful when used in combination with anticancer drugs. Furthermore, since the operating steps are simple, there is no decrease in activity, yield, or enzyme decomposition during purification, making it an extremely excellent method. According to the method of the present invention, it is estimated that extremely effective purification of urokinase can be achieved through the following separation process.
【表】
アフイニテイクロマト
[Table] Affinity Chromato
Claims (1)
糖体顆粒に接触させ、そのように処理した溶液を
合成ウロキナーゼ阻害剤を炭素鎖を介して多糖体
顆粒と結合せしめてなる担体と接触させてウロキ
ナーゼを吸着させ、しかる後吸着されたウロキナ
ーゼを溶離回収することを特徴とする、ウロキナ
ーゼの精製法。1. A buffer solution of crude urokinase is brought into contact with ion-exchanged polysaccharide granules, and the thus treated solution is brought into contact with a carrier made of a synthetic urokinase inhibitor bound to the polysaccharide granules via carbon chains to adsorb urokinase. , and then elution and recovery of the adsorbed urokinase.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16579878A JPS5592687A (en) | 1978-12-28 | 1978-12-28 | Purification of urokinase |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16579878A JPS5592687A (en) | 1978-12-28 | 1978-12-28 | Purification of urokinase |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5592687A JPS5592687A (en) | 1980-07-14 |
| JPS6215196B2 true JPS6215196B2 (en) | 1987-04-06 |
Family
ID=15819185
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16579878A Granted JPS5592687A (en) | 1978-12-28 | 1978-12-28 | Purification of urokinase |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5592687A (en) |
-
1978
- 1978-12-28 JP JP16579878A patent/JPS5592687A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5592687A (en) | 1980-07-14 |
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