JPH0558709B2 - - Google Patents
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- Publication number
- JPH0558709B2 JPH0558709B2 JP59241457A JP24145784A JPH0558709B2 JP H0558709 B2 JPH0558709 B2 JP H0558709B2 JP 59241457 A JP59241457 A JP 59241457A JP 24145784 A JP24145784 A JP 24145784A JP H0558709 B2 JPH0558709 B2 JP H0558709B2
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- Prior art keywords
- precursor
- cells
- medium
- acid
- present
- Prior art date
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Description
〔産業上の利用分野〕
本発明は、プラスミノーゲンアクチベーター前
駆体(以下、前駆体という)の産生増強方法に関
する。更に詳しくは、本発明は、前駆体の産生細
胞を培養して前駆体を生産するに際して、培地に
中性アミノ酸及び有機酸もしくはその塩を含むこ
とを特徴とする前駆体の産生増強方法に関する。
〔従来の技術〕
本発明の前駆体は、先に本発明者が見出したも
のであり、その詳細は特願昭58−170354号に記載
されている。すなわち、本前駆体はそのままでは
不活性であるが、プラスミン処理することにより
酵素活性を発現する、いわゆるチモゲンの一種で
ある。この前駆体はヒト腎細胞に無血清培地中に
て生成できることが最近判明した。本前駆体はア
ミノ酸411個の鎖状構造を有しており、分子量5
万、フイブリンに特異的な親和性を示し、従来の
ウロキナーゼとは全く異なる性質を有する。ま
た、合成基質法では活性が認められず、平板法で
活性を示す。その産生条件については、特願昭58
−170354号で詳細に述べられているが、必ずし
も、その産生効率が充分であるとは言えない。
〔発明が解決しようとする問題点〕
従つて、本発明の目的は前駆体の産生増強方法
を提供することである。
〔問題点を解決するための手段〕
そこで本発明者らは、上記目的を解決するため
に、前駆体の産生増強について鋭意検討した結
果、前駆体産生性細胞培養培地中に、中性アミノ
酸並びに有機酸またはその塩をそれぞれ高濃度含
ませることにより、前駆体の産生を向上できるこ
とを見いだし、本発明を完成した。
即ち、本発明はプラスミノーゲンアクチベータ
ー前駆体の産生細胞を培養して、プラスミノーゲ
ンアクチベーター前駆体を生産するに際して、培
地に中性アミノ酸を0.16〜3.06w/v%、並びに
有機酸またはその塩を0.10〜3.00w/v%含むこ
とを特徴とするプラスミノーゲンアクチベーター
前駆体の産生増強方法に関する。
(1) 前駆体産生細胞の調製
前駆体産生細胞の原料としては、ヒト腎細胞が
好適に用いられる。たとえば、ヒト腎細胞より得
たprimary cultureまたはdipioid cellsを継代培
養して得られる前駆体を産生する細胞が用いられ
る。この種細胞を20万〜30万cells/ml植え込み、
培地(たとえば、waymouth培地あるいは
Dulbecco´s modified MEM培地に熱不活化牛胎
児血清2〜5w/v%を添加したもの)を用いて
2〜3日間培養を続けた後、必要ならば培地を新
しく交換して継代培養し、細胞数を100万〜200万
cells/mlに調整する。
(2) 培養条件
基本培地としては、たとえばwaymouth培地あ
るいはDulbecco´s modified MEM培地に0.05〜
0.2w/v%ヒト血清アルブミンを添加した無血
清培地が用いられる。
これに本発明の特徴である、中性アミノ酸並び
に有機酸またはその塩が添加される。中性アミノ
酸としてはグリシン、アラニン、ロイシン、イソ
ロイシン、フエニルアラニン等の脂肪族アミノ酸
などが例示されるが、好適にはグリシンが用いら
れる。添加量としては0.1〜3w/v%が例示され
る。添加量が、0.1%以下では産生能が十分上が
らず、また、3%以上では、毒性が上がつて産生
能向上にはマイナスとなるためである。また、中
性アミノ酸と有機酸又はその塩の割合としては、
1:10〜10:1(重量比)程度が望ましい。有機
酸としては炭素数3〜18のものであれば特に限定
されない。通常は、カルボン酸、特に飽和または
不飽和脂肪族カルボン酸(就中、モノカルボン酸
またはジカルボン酸)が好適に使用される。当該
有機酸は置換基として、たとえば水酸基等を有し
ていてもよい。かかる有機酸としては、フマル
酸、コハク酸、リンゴ酸、クエン酸、ステアリン
酸、オレイン酸、リノール酸、パルミチン酸、リ
ノレン酸、ミリスチン酸などが例示される。特に
好適には、コハク酸などの脂肪族ジカルボン酸が
使用される。上記有機酸の塩としては、生理的に
受け入れられる塩、たとえばアルカリ金属塩(ナ
トリウム塩、カリウム塩など)、アルカリ土類金
属塩(カルシウム塩など)などを用いることがで
きる。これらの有機酸もしくはその塩の添加量と
しては0.1〜3w/v%が例示される。
また他に添加物として公知であるラクトアルブ
ミン水解物、トランスフエリン、インシユリン等
のホルモンなどを添加してよい。
培養は、例えば前駆体産生細胞50万〜200万
cells/mlを一定に維持しながら、上記培地中で
行つて、前駆体を産生させ、2〜3日毎に培養培
地を新しく交換する。そしてこの交換した培地中
に存在する前駆体を回収する。
培地からの前駆体の回収は公知の手段を用いて
行えばよく、例えば当該培地を遠心分離、減圧濃
縮、塩析分画、ゲル濾過、濃縮、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
ーを、便宜組み合わせることによつて行われる。
〔発明の効果〕
本発明の方法により、本前駆体の産生は従来の
方法に比べて活性比で約1.3〜3倍程度増強する
ことができる。
実験例 1
本発明による前駆体産生増強効果を見るため
に、前駆体の産生量の比較実験を行つた。第1表
に示したようにグリシン及びコハク酸の添加量は
0〜5.0w/v%の範囲で設定した。それ以外の
条件は実施例1に準じて各群とも同様に行つた。
産生量の指標として活性を測定した。
活性量の測定は、p−MCA法により以下のよ
うに行つた。即ち、検体0.1mlとプラスミン溶液
(0.2cu/ml、ゼラチン緩衝液〔PH8.6〕で調製し
たもの)0.1mlを混合後、37℃で10分間インキユ
ベーシヨンし、p−MCA溶液(0.1mMGlu−
Gly−Arg−MCA)1mlを加え、さらに37℃で20
分間インキユベーシヨンし、18v/v%酢酸を加
えて反応を止めた後、Ex(励起波長)370nm、
Em(螢光波長)460nmにて螢光強度を測定した。
その結果は、第1表に示す通りである。
なお単位はU/mlを用いた。Uはウロキナーゼ
国際単位であり、1U/mlは検体1mlにつきプラ
スミン処理によつて発現する線維素溶解活性が
1Uに相当することを意味する。
実験例 2
実験例1と同様にして第2表に記載の添加物に
ついて、併用効果を検討し、その結果を第2表に
示した。
実施例 1
ヒト腎臓細胞より得たprimary−cultureを培
養し、本発明前駆体を産生する細胞だけを分離後
再培養し、その20×104cells/mlの濃度で熱不活
化ウシ胎児血清5w/v%含有Waymouth培地に
埋え込み、3日間培養後、細胞数が100×
104cells/mlとなつた時点で、さらに、0.1w/v
%ヒト血清アルブミン、0.5w/v%グリシン、
0.5w/v%コハク酸ナトリウム含有Waymouth
培地(無血清培地)に上記前駆体産生細胞100×
104cells/mlを植え直し、この濃度を維持しつつ
3日間培養した。培養液を遠心分離し、沈澱には
新しい培地を添加して培養を続けた。上清中には
前駆体(活性は1ml当たり300Uに相当)が含ま
れていた。
本発明により得られた前駆体は、特開昭58−
170354で開示した「繊維素溶解酵素前駆体」と全
く同一の性質を有していた。
実施例 2
実施例1により得られた前駆体を含む培養上清
をPH5.5に調整した後、CM−Sephade×C−50に
接触した。0.16Mリン酸緩衝液(PH8.5)で吸着
していた前駆体を溶出させた。
一方、前駆体で予め免疫しておいたマウス
BALB/cの脾臓細胞とマウスミエローマ細胞
をポリエチレングリコールにより融合させたハイ
ブリドーマのうち、前駆体に体する抗体産生の高
いクローンを選択した。この融合細胞の培養液か
ら、前駆体モノクローナル抗体を回収した。この
モノクローナル抗体をCNBr活性化Sepharose
4B(Pharmacia社)に固定した。
このモノクローナル抗体カラムを0.4M NaCl
含有0.1Mリン酸緩衝液(PH7.0)で平衡化し、こ
れに前記の前駆体を含有する溶出液を接触した。
0.4M NaCl含有0.1Mリン酸緩衝液(PH7.0)でカ
ラムを洗浄した後、吸着していた当該前駆体を
0.5M NaCl含有0.2Mグリシン−HCl水溶液(PH
2.5)で溶出させた。溶出液を除菌濾過した後、
凍結乾燥し比活性が少なくとも80000U/mgの高
度精製前駆体を得た。
なお、この精製品はSDS−ポリアクリルアミド
ゲル電気泳動法より分子量5万の1本の帯を示し
た。
[Industrial Application Field] The present invention relates to a method for enhancing the production of a plasminogen activator precursor (hereinafter referred to as a precursor). More specifically, the present invention relates to a method for enhancing production of a precursor, which comprises containing a neutral amino acid and an organic acid or a salt thereof in a medium when producing a precursor by culturing precursor producing cells. [Prior Art] The precursor of the present invention was previously discovered by the present inventor, and its details are described in Japanese Patent Application No. 170354/1982. That is, this precursor is inactive as it is, but it is a type of so-called zymogen that expresses enzymatic activity when treated with plasmin. It has recently been found that this precursor can be produced in human kidney cells in serum-free medium. This precursor has a chain structure of 411 amino acids and has a molecular weight of 5.
However, it shows specific affinity for fibrin and has properties completely different from conventional urokinase. Furthermore, no activity was observed in the synthetic substrate method, but activity was observed in the plate method. Regarding its production conditions, please refer to the patent application filed in 1983.
Although it is described in detail in No.-170354, the production efficiency cannot necessarily be said to be sufficient. [Problems to be Solved by the Invention] Therefore, an object of the present invention is to provide a method for enhancing production of a precursor. [Means for Solving the Problems] Therefore, in order to solve the above object, the present inventors conducted intensive studies on enhancing production of precursors, and found that neutral amino acids and The present invention was completed based on the discovery that the production of precursors can be improved by containing organic acids or their salts at high concentrations. That is, in the present invention, when producing a plasminogen activator precursor by culturing plasminogen activator precursor producing cells, 0.16 to 3.06 w/v% of neutral amino acids and organic acids or The present invention relates to a method for enhancing production of a plasminogen activator precursor, characterized in that the salt thereof is contained in an amount of 0.10 to 3.00 w/v%. (1) Preparation of precursor-producing cells Human kidney cells are preferably used as a raw material for precursor-producing cells. For example, cells that produce precursors obtained by subculturing primary culture or dipioid cells obtained from human kidney cells are used. Inject 200,000 to 300,000 cells/ml of this type of cells,
medium (e.g. waymouth medium or
After continuing culturing for 2-3 days using Dulbecco's modified MEM medium supplemented with 2-5% w/v of heat-inactivated fetal bovine serum, if necessary, replace the medium with a new one and subculture. , cell number 1 million to 2 million
Adjust to cells/ml. (2) Culture conditions As a basic medium, for example, Waymouth medium or Dulbecco's modified MEM medium with 0.05~
A serum-free medium supplemented with 0.2% w/v human serum albumin is used. A neutral amino acid and an organic acid or a salt thereof, which are characteristics of the present invention, are added to this. Examples of neutral amino acids include aliphatic amino acids such as glycine, alanine, leucine, isoleucine, and phenylalanine, but glycine is preferably used. An example of the amount added is 0.1 to 3 w/v%. This is because if the amount added is less than 0.1%, the productivity will not increase sufficiently, and if it is more than 3%, the toxicity will increase, which will have a negative effect on improving the productivity. In addition, the ratio of neutral amino acids to organic acids or their salts is as follows:
A ratio of about 1:10 to 10:1 (weight ratio) is desirable. The organic acid is not particularly limited as long as it has 3 to 18 carbon atoms. Usually, carboxylic acids, especially saturated or unsaturated aliphatic carboxylic acids (especially monocarboxylic acids or dicarboxylic acids) are preferably used. The organic acid may have, for example, a hydroxyl group as a substituent. Examples of such organic acids include fumaric acid, succinic acid, malic acid, citric acid, stearic acid, oleic acid, linoleic acid, palmitic acid, linolenic acid, myristic acid, and the like. Particular preference is given to using aliphatic dicarboxylic acids such as succinic acid. As the salt of the organic acid, physiologically acceptable salts such as alkali metal salts (sodium salts, potassium salts, etc.), alkaline earth metal salts (calcium salts, etc.), etc. can be used. The amount of these organic acids or salts added is exemplified in the range of 0.1 to 3 w/v%. In addition, known additives such as hormones such as lactalbumin hydrolyzate, transferrin, and insulin may be added. For example, 500,000 to 2 million precursor-producing cells are cultured.
The cells/ml are maintained constant in the above medium to produce precursors, and the culture medium is replaced every 2-3 days. The precursors present in this replaced medium are then recovered. Recovery of the precursor from the medium may be performed using known means, such as centrifugation, vacuum concentration, salting out fractionation, gel filtration, concentration, ion exchange chromatography, and affinity chromatography. , by convenient combinations. [Effects of the Invention] According to the method of the present invention, the production of the present precursor can be enhanced by about 1.3 to 3 times in terms of activity ratio compared to conventional methods. Experimental Example 1 In order to examine the effect of enhancing precursor production according to the present invention, an experiment was conducted to compare the production amount of precursors. As shown in Table 1, the amounts of glycine and succinic acid added were set in the range of 0 to 5.0 w/v%. The other conditions were the same as in Example 1 for each group.
Activity was measured as an indicator of production amount. The amount of activity was measured by the p-MCA method as follows. That is, after mixing 0.1 ml of the specimen and 0.1 ml of plasmin solution (0.2 cu/ml, prepared with gelatin buffer [PH8.6]), incubation at 37°C for 10 minutes, and p-MCA solution (0.1 mMGlu-
Add 1 ml of Gly-Arg-MCA) and further heat for 20 minutes at 37°C.
After incubating for minutes and stopping the reaction by adding 18v/v% acetic acid, Ex (excitation wavelength) 370nm,
The fluorescence intensity was measured at Em (fluorescence wavelength) of 460 nm.
The results are shown in Table 1. Note that the unit used was U/ml. U is the international unit of urokinase, and 1U/ml is the fibrinolytic activity expressed by plasmin treatment per ml of sample.
It means equivalent to 1U. Experimental Example 2 Similar to Experimental Example 1, the effects of combined use of the additives listed in Table 2 were investigated, and the results are shown in Table 2. Example 1 A primary culture obtained from human kidney cells was cultured, and only cells producing the precursor of the present invention were isolated and re-cultured, and 5w of heat-inactivated fetal bovine serum was added at a concentration of 20×10 4 cells/ml. /v% containing Waymouth medium, and after 3 days of culture, the number of cells decreased to 100x.
10 4 cells/ml, further increase 0.1w/v
% human serum albumin, 0.5w/v% glycine,
Waymouth containing 0.5w/v% sodium succinate
Add the above precursor producing cells 100x to the medium (serum-free medium)
The cells were replanted at 10 4 cells/ml and cultured for 3 days while maintaining this concentration. The culture solution was centrifuged, fresh medium was added to the precipitate, and culture was continued. The supernatant contained the precursor (activity equivalent to 300 U/ml). The precursor obtained according to the present invention is
It had exactly the same properties as the "fibrinolytic enzyme precursor" disclosed in No. 170354. Example 2 The culture supernatant containing the precursor obtained in Example 1 was adjusted to pH 5.5 and then brought into contact with CM-Sephade×C-50. The adsorbed precursor was eluted with 0.16M phosphate buffer (PH8.5). On the other hand, mice pre-immunized with the precursor
Among the hybridomas obtained by fusing BALB/c spleen cells and mouse myeloma cells with polyethylene glycol, clones with high antibody production based on the precursor were selected. A precursor monoclonal antibody was recovered from the culture solution of this fused cell. This monoclonal antibody was transferred to CNBr-activated Sepharose.
4B (Pharmacia). This monoclonal antibody column was washed with 0.4M NaCl.
The solution was equilibrated with a 0.1M phosphate buffer (PH7.0), and the eluate containing the precursor was contacted therewith.
After washing the column with 0.1M phosphate buffer (PH7.0) containing 0.4M NaCl, remove the adsorbed precursor.
0.2M glycine-HCl aqueous solution containing 0.5M NaCl (PH
2.5). After sterilizing and filtering the eluate,
A highly purified precursor with a specific activity of at least 80000 U/mg was obtained by lyophilization. This purified product showed one band with a molecular weight of 50,000 by SDS-polyacrylamide gel electrophoresis.
【表】【table】
【表】【table】
Claims (1)
生細胞を培養して、プラスミノーゲンアクチベー
ター前駆体を生産するに際して、培地に中性アミ
ノ酸を0.16〜3.06w/v%、並びに有機酸または
その塩を0.10〜3.00w/v%含むことを特徴とす
るプラスミノーゲンアクチベーター前駆体の産生
増強方法。1. When culturing plasminogen activator precursor producing cells to produce plasminogen activator precursor, add 0.16 to 3.06 w/v% of neutral amino acids and 0.10% of organic acid or its salt to the medium. A method for enhancing production of a plasminogen activator precursor, characterized in that it contains ~3.00w/v%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59241457A JPS61119189A (en) | 1984-11-15 | 1984-11-15 | Step-up production of plasminogen activator precursor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59241457A JPS61119189A (en) | 1984-11-15 | 1984-11-15 | Step-up production of plasminogen activator precursor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61119189A JPS61119189A (en) | 1986-06-06 |
| JPH0558709B2 true JPH0558709B2 (en) | 1993-08-27 |
Family
ID=17074595
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59241457A Granted JPS61119189A (en) | 1984-11-15 | 1984-11-15 | Step-up production of plasminogen activator precursor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61119189A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6384490A (en) * | 1986-09-29 | 1988-04-15 | Green Cross Corp:The | Production enhancing method for plasminogen activator precursor |
| AU783954B2 (en) | 2000-05-10 | 2006-01-05 | Asubio Pharma Co., Ltd. | Method of inhibiting the formation of by-product in the production of genetically modified polypeptide |
-
1984
- 1984-11-15 JP JP59241457A patent/JPS61119189A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61119189A (en) | 1986-06-06 |
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