JPH04634B2 - - Google Patents

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Publication number
JPH04634B2
JPH04634B2 JP58237636A JP23763683A JPH04634B2 JP H04634 B2 JPH04634 B2 JP H04634B2 JP 58237636 A JP58237636 A JP 58237636A JP 23763683 A JP23763683 A JP 23763683A JP H04634 B2 JPH04634 B2 JP H04634B2
Authority
JP
Japan
Prior art keywords
urokinase
antibody
specific activity
purified
immobilized
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 - Lifetime
Application number
JP58237636A
Other languages
Japanese (ja)
Other versions
JPS60130526A (en
Inventor
Masakazu Tajima
Yatsuhiro Kamimura
Hirobumi Arimura
Masayuki Nishida
Takehiko Kawano
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.)
GREEN CROSS CORP
Original Assignee
GREEN CROSS CORP
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by GREEN CROSS CORP filed Critical GREEN CROSS CORP
Priority to JP58237636A priority Critical patent/JPS60130526A/en
Publication of JPS60130526A publication Critical patent/JPS60130526A/en
Publication of JPH04634B2 publication Critical patent/JPH04634B2/ja
Granted legal-status Critical Current

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  • Enzymes And Modification Thereof (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
  • Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
  • Peptides Or Proteins (AREA)

Description

【発明の詳細な説明】 本発明は、酵素にて処理された抗体をリガンド
とするアフイニテイクロマトグラフイーを使用す
る、前記抗体に対応する抗原物質の精製方法に関
する。更に詳しくは、本発明は、抗原、抗体の機
作を用いて、精製しようとする抗原物質に対して
特異性のある免疫抗体を酵素処理することによ
り、特異性の非常に高い修飾精製抗体とし、これ
を不溶性担体に固定せしめ、この親和性の高い固
定化担体により粗製抗原物質から高純度、高回収
率に抗原物質を製造する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for purifying an antigenic substance corresponding to an enzyme-treated antibody using affinity chromatography using the antibody as a ligand. More specifically, the present invention uses the mechanisms of antigens and antibodies to enzymatically treat immune antibodies specific to the antigen substance to be purified, thereby producing modified purified antibodies with extremely high specificity. , relates to a method for producing an antigenic substance from a crude antigenic substance with high purity and high recovery rate by immobilizing it on an insoluble carrier and using this immobilized carrier with high affinity.

例えば、ウロキナーゼは血液中に存在するプラ
スミノゲンをプラスミンへ活性化する線溶系酵素
である。従つて、これを人体へ注射することによ
り血管内に生じた血栓を溶解するので、脳血栓、
その他の血栓症の治療に有効である以外に、制癌
剤としても併用することにより治療効果が上が
り、その有用性が広がつている。
For example, urokinase is a fibrinolytic enzyme that activates plasminogen present in the blood into plasmin. Therefore, by injecting this into the human body, it dissolves blood clots that occur in blood vessels, thereby preventing cerebral thrombosis,
In addition to being effective in the treatment of other thromboses, the therapeutic effect is increased when used in combination as an anticancer agent, and its usefulness is expanding.

特に、人尿から採取し精製したウロキナーゼ
は、副作用がほとんどないことにより医薬品とし
て現在広く用いられている。
In particular, urokinase collected from human urine and purified is currently widely used as a medicine because it has almost no side effects.

従来、ウロキナーゼの精製には、シリカゲル、
ハイフロスーパーセル、ゼオライトアクリルニト
リル、硫酸バリウム、あるいは各種イオン交換体
とゲル濾過および対応する抗体を用いた抗ウロキ
ナーゼ抗体を固定化した免疫吸着体が用いられて
いる。
Traditionally, urokinase was purified using silica gel,
Hyflo Super Cell, zeolite acrylonitrile, barium sulfate, or various ion exchangers and gel filtration are used, as well as immunoadsorbents in which anti-urokinase antibodies are immobilized using the corresponding antibodies.

また、B型肝炎表面抗原(HBsAg)も高純度
化し、不活化処理を行なつたものはB型肝炎ワク
チンとして利用できる。
Hepatitis B surface antigen (HBsAg) can also be highly purified and inactivated and used as a hepatitis B vaccine.

HBsAgの精製法としては、硫安、エアロジル、
イオン交換樹脂、ゲル濾過、超遠心分離、対応す
る抗体を用いた抗HBsAg抗体を固定化した免疫
吸着体を用いる方法が用いられる。
HBsAg purification methods include ammonium sulfate, Aerosil,
Methods using an ion exchange resin, gel filtration, ultracentrifugation, and an immunoadsorbent immobilized with an anti-HBsAg antibody using the corresponding antibody are used.

そこで本発明者等は、これらの公知の精製方法
に比較して、更に優れた精製方法を種々検討した
結果、既知のいずれの精製方法よりも優れた精製
効率を有し、操作が簡単で、しかも繰り返し使用
できる粗製抗原物質の精製方法を見いだした。
Therefore, the present inventors have investigated various purification methods that are better than these known purification methods, and have found that they have a purification efficiency that is superior to any known purification method, are easy to operate, Furthermore, we have discovered a method for purifying crude antigenic substances that can be used repeatedly.

即ち、抗体には一般に、他の夾雑蛋白、糖など
が結合しており、抗体を通常の精製方法、例えば
陰イオン交換体にて精製しても、これらの夾雑蛋
白、糖などの不純物を切断、分解することができ
ない。
In other words, antibodies generally have other contaminant proteins, sugars, etc. bound to them, and even if antibodies are purified using normal purification methods, such as anion exchangers, these contaminant proteins, sugars, and other impurities cannot be cleaved. , cannot be disassembled.

ところが、抗体を適当な条件下、特定の酵素を
組み合わせて処理すれば、これら不純物を除去す
ることができ、しかもかかる処理抗体をアフイニ
テイクロマトグラフイーにおける吸着体のリガン
ドとし、当該抗体に対抗する抗原物質の精製に使
用すれば、高収率、高純度で抗原物質が回収され
ることを見出した。
However, these impurities can be removed by treating antibodies with a combination of specific enzymes under appropriate conditions, and the treated antibodies can be used as adsorbent ligands in affinity chromatography to counteract the antibodies. It has been found that when used to purify antigenic substances, the antigenic substances can be recovered in high yield and with high purity.

本発明は、かかる新知見に基づいて完成された
ものであり、ペプシン、トリプシン、プラスミン
から選ばれる少なくとも蛋白分解酵素、およびア
ミラーゼ、アルギナーゼから選ばれる少なくとも
一の糖分解酵素にて処理された抗体を固定化した
担体を吸着体することによる、前記抗体に対応す
る抗原物質の精製方法に関する。
The present invention was completed based on this new knowledge, and provides an antibody treated with at least a proteolytic enzyme selected from pepsin, trypsin, and plasmin, and at least one glycolytic enzyme selected from amylase and arginase. The present invention relates to a method for purifying an antigenic substance corresponding to the antibody by adsorbing an immobilized carrier.

本発明によれば、高純度、高収率で抗原物質が
得られ、しかも操作が簡単である他、大規模製造
時での免疫抗体の固定化不溶性担体の機能向上と
生物学的安定性(腐敗、発熱性物質の発生の防止
等)の向上が図られる。
According to the present invention, antigenic substances can be obtained with high purity and high yield, and the operation is simple. In addition, the present invention improves the functionality of an insoluble carrier on which immune antibodies are immobilized during large-scale production, and improves biological stability ( (prevention of spoilage, generation of pyrogenic substances, etc.) will be improved.

本発明における精製対象である抗原物質には、
特に制限はなく、動物に免疫して、抗体を生成し
うるものであればよく、たとえばウロキナーゼ、
HBsAg、カリクレイン、インターフイエロンな
どがあげられる。
The antigenic substances to be purified in the present invention include:
There are no particular limitations, as long as it can be used to immunize animals and produce antibodies, such as urokinase,
Examples include HBsAg, kallikrein, and interferon.

本発明に用いられる抗体は、前記抗原に対応す
る抗体であり、酵素処理を付す際には、必ずしも
高度精製品でなくてもよく、たとえば免疫動物の
血漿、血清などであつてもよい。又、モノクロー
ナル抗体も好適に利用される。
The antibody used in the present invention is an antibody corresponding to the above-mentioned antigen, and when subjected to enzyme treatment, it does not necessarily have to be a highly purified product, and may be, for example, plasma or serum from an immunized animal. Furthermore, monoclonal antibodies are also preferably used.

酵素処理に用いられる酵素は、ペプシン、トリ
プシン、プラスミンの蛋白分解酵素、およびアミ
ラーゼ、アルギナーゼの糖分解酵素であり、少な
くとも一の蛋白分解酵素および糖分解酵素を組み
合わせて処理すればよい。
The enzymes used in the enzyme treatment are proteases such as pepsin, trypsin, and plasmin, and glycolytic enzymes such as amylase and arginase, and the treatment may be performed by combining at least one protease and glycolytic enzyme.

酵素処理は個々の示適条件下で行われ、その条
件は、たとえば次の通りである。
Enzyme treatment is carried out under individually suitable conditions, such as the following conditions.

例えば、抗体純度に応じて抗体の0.1μg〜1mg
当たり、ペプシン、トリプシン、プラスミンの場
合は、0.1〜100μg/mlを使用して、PH2〜4.5に
て25〜37℃で10〜30時間処理、β−アミラーゼの
場合は0.1μg〜100μgを使用してPH5.5〜8.5にて、
25〜37℃で10〜30時間処理、アルギナーゼの場合
は0.1μg〜100μgを加えて、PH7.5〜10にて、25
〜37℃で10〜30時間の処理を行う。
For example, 0.1 μg to 1 mg of antibody depending on antibody purity
For pepsin, trypsin, and plasmin, use 0.1 to 100 μg/ml and treat at PH2 to 4.5 at 25 to 37°C for 10 to 30 hours, and for β-amylase, use 0.1 μg to 100 μg. At PH5.5-8.5,
Treat at 25-37℃ for 10-30 hours, add 0.1μg-100μg of arginase, and incubate at pH7.5-10 for 25 hours.
Perform processing for 10-30 h at ~37 °C.

この酵素処理後、一般には透析、濃縮及び/又
は、限外濾過により濃縮してゲル濾過を行つて、
E280nmの高い部分について赤血球凝集反応法に
よる抗ウロキナーゼのHAI法による測定を行い
プールする。
After this enzyme treatment, it is generally concentrated by dialysis, concentration and/or ultrafiltration, and gel filtration is performed.
E Measure the high part of 280 nm using the HAI method for anti-urokinase using the hemagglutination method and pool.

かくして得られた抗体を固定させるための担体
としては、従来既知の固定化担体がいずれも好適
に使用しうる。具体的には、たとえば精製寒天ゲ
ル、セルロース誘導体、デキストラン重合物、ポ
リアクリルアミド等の重合物のゲル、ガラス粒子
などが例示される。
As a carrier for immobilizing the antibody thus obtained, any conventionally known immobilization carrier can be suitably used. Specific examples include purified agar gel, cellulose derivatives, dextran polymers, gels of polymers such as polyacrylamide, and glass particles.

抗体の担体への固定化は、従来既知の方法
〔Cuatrecasasらの方法(P.Cuaftrecasas,J.
Biol.Chem.,245,3059(1970)〕、またはこれに
準ずる方法にて行えばよい。
The antibody can be immobilized on a carrier by a conventionally known method [Cuatrecasas et al.'s method (P. Cuaftrecasas, J.
Biol.Chem., 245 , 3059 (1970)] or a method similar thereto.

本方法によれば、非常に比活性の高い純品を回
収率85%以上で得ることができて、その特異性は
非常に良く、高分子ウロキナーゼの抗体を使用し
た場合、100%近い高分子ウロキナーゼが回収で
きた。
According to this method, a pure product with extremely high specific activity can be obtained with a recovery rate of 85% or more, and its specificity is very good. Urokinase was recovered.

同様に、HBsAgも酵素処理して使用した場合
も高回収、高純度の回収を得た。
Similarly, when HBsAg was used after enzyme treatment, high recovery and high purity recovery were obtained.

以下に実施例を示すが、本発明はこれらに限定
されない。
Examples are shown below, but the present invention is not limited thereto.

実施例 1 公知の方法で精製したウロキナーゼの比活性、
80000単位/E280nm以上のものの、10〜20万単
位/mlとFreunds complete adjuvantを均等混合
する。
Example 1 Specific activity of urokinase purified by a known method,
80,000 units/E 100,000 to 200,000 units/ml of 280 nm or more and Freunds complete adjuvant are evenly mixed.

この1mlを3〜4Kgの家兎に皮下、または皮内
注射し、以後4〜6週間毎に0.5mlずつを同様追
加免疫して、その後抗ウロキナーゼ価を赤血球凝
集反応法(HAI法)で測定し値の上がつた時点
で家兎の耳静脈より1回に50mlずつ採血した。
Inject 1 ml of this subcutaneously or intradermally into a 3-4 kg domestic rabbit, then boost 0.5 ml in the same manner every 4-6 weeks, and then measure the anti-urokinase titer using the hemagglutination assay (HAI method). When the level rose, 50ml of blood was collected from the ear vein of the rabbit at a time.

この抗血清100mlに、まず硫安12gを加え、そ
の遠心上清へPH7.2にて13gを追加して沈澱物を
遠心分離で得た。
First, 12 g of ammonium sulfate was added to 100 ml of this antiserum, and 13 g was added to the centrifuged supernatant at pH 7.2 to obtain a precipitate by centrifugation.

この沈澱物を0.03M食塩を含む0.04Mリン酸緩
衝液のPH8.0E280nmの吸光度で2付近まで溶解し
た。
This precipitate was dissolved at pH 8.0E in a 0.04M phosphate buffer containing 0.03M sodium chloride to an absorbance of around 2 at 280 nm.

そして、この溶液を同一緩衝液で平衡化した
DEAE−セルロース70ml(直径3cm、高さ10cm)
カラムを通過して、抗ウロキナーゼ部分をHAI
法とE280nmで測定して、高純度抗ウロキナーゼ
画分、約1gを得た。
This solution was then equilibrated with the same buffer.
DEAE-cellulose 70ml (diameter 3cm, height 10cm)
HAI the anti-urokinase moiety by passing it through the column
Approximately 1 g of a highly purified anti-urokinase fraction was obtained as measured by E 280 nm.

この抗ウロキナーゼ画分の40mg当たり、PH3.5
にてペプシン1μg/終濃度として37℃で18時間
の反応を行い、次いで1N−NaOHでPH6.5に調製
後、β−アミラーゼを5μg/終濃度にして、25
℃で12時間処理して、最後にPH9.2にてアルギナ
ーゼの1μg/終濃度を加えて25℃、18時間の処
理後、室温にてPH10で1時間放置して、0.3M食
塩加0.01Mリン酸緩衝液PH8.5にて透析、濃縮し
て、それと同一緩衝液のセフアクリルS−500に
てゲル濾過して、PHA法にて抗ウロキナーゼ分
画として約0.4g相当を得た。
Per 40 mg of this anti-urokinase fraction, PH3.5
The reaction was carried out at 37°C for 18 hours with pepsin at 1 μg/final concentration, and then the pH was adjusted to 6.5 with 1N-NaOH, and β-amylase was adjusted to 5 μg/final concentration at 25°C.
℃ for 12 hours, and finally at pH 9.2, add 1 μg/final concentration of arginase. After treatment at 25℃ for 18 hours, leave at room temperature for 1 hour at PH 10, add 0.3M NaCl, and add 0.01M of arginase. The product was dialyzed and concentrated using a phosphate buffer pH 8.5, gel-filtered using the same buffer as Sephacryl S-500, and an anti-urokinase fraction equivalent to about 0.4 g was obtained using the PHA method.

この酵素処理液のE280nmを、5付近に0.1M炭
酸ソーダ緩衝液PH9を希釈して、ほぼ等量の
CNBr−activated Sepharose 4B(フアルアシア
製)を加えて、4℃で24時間ゆつくりと撹拌し
た。
E 280 nm of this enzyme-treated solution was diluted with 0.1M sodium carbonate buffer PH9 to around 5 to give an approximately equal amount of E 280 nm.
CNBr-activated Sepharose 4B (manufactured by Phalasia) was added, and the mixture was gently stirred at 4°C for 24 hours.

この間、最初のHAI値は、1:2000から1:
2付近に混合液は低下し、カツプリングが順調に
進んだことが判つた。
During this time, the initial HAI value changed from 1:2000 to 1:
The mixed liquid decreased to around 2, indicating that the coupling progressed smoothly.

反応終了後、0.15M食塩加0.02Mホウ酸緩衝液
PH8にて充分洗浄して、酵素処理した修飾抗ウロ
キナーゼ固定Sepharose 4Bを得た。
After the reaction is complete, add 0.02M borate buffer with 0.15M sodium chloride.
After thorough washing at PH8, enzyme-treated modified anti-urokinase-immobilized Sepharose 4B was obtained.

本品1ml当たり、比活性3000単位/E280nmの
粗製ウロキナーゼは約300000単位を吸着すること
が出来て、同一緩衝液で洗浄後、0.5M食塩加
0.17Mグリシン緩衝液にて溶出して、比活性
85000単位/E280nm以上、回収率95%以上を得
た。
Approximately 300,000 units of crude urokinase with a specific activity of 3,000 units/E 280 nm can be adsorbed per ml of this product, and after washing with the same buffer, 0.5M sodium chloride was added.
Elute with 0.17M glycine buffer and determine specific activity.
More than 85000 units/E 280 nm and a recovery rate of more than 95% were obtained.

同様に、比活性1000単位/E280nmの組織培養
ウロキナーゼも約200000単位が吸着し、比活性
100000単位/E280nmで、回収率95%以上を得た。
Similarly, about 200,000 units of tissue culture urokinase with a specific activity of 1000 units/E 280 nm were adsorbed, and the specific activity was 1000 units/E 280 nm.
A recovery rate of 95% or more was obtained at 100,000 units/E 280 nm.

なお、酵素処理を行わない抗体による抗ウロキ
ナーゼ固定Sepharose 4Bでの精製では吸着率が
劣り、とりわけ比活性の上昇が500000単位/
E280nmを上がらず、回収率80%程度を示した。
In addition, purification using anti-urokinase-immobilized Sepharose 4B using an antibody without enzyme treatment has poor adsorption rate, especially the increase in specific activity of 500,000 units/
E did not exceed 280 nm, and the recovery rate was approximately 80%.

実施例 2 実施例1にて調製された、酵素処理した修飾抗
ウロキナーゼ固定Sepharose 4Bを用いて、本品
1ml当り、組織培養ウロキナーゼの培養液の約
10000単位を吸着することが出来て、比活性とし
て90000単位/E280nm以上のものを回収率95%で
得た。
Example 2 Using the enzyme-treated modified anti-urokinase immobilized Sepharose 4B prepared in Example 1, approximately 1 ml of the tissue culture urokinase culture solution was added per 1 ml of this product.
It was possible to adsorb 10,000 units, and a specific activity of 90,000 units/E 280 nm or more was obtained with a recovery rate of 95%.

尚、酵素処理を行わない抗体による抗ウロキナ
ーゼ固定Sepharose 4Bでの精製では吸着率が劣
り、とりわけ比活性の上昇が75000単位/E280nm
で回収率が75%を示した。
In addition, purification using anti-urokinase-immobilized Sepharose 4B using an antibody without enzyme treatment has poor adsorption rate, and in particular, the increase in specific activity is 75,000 units/E 280 nm.
The recovery rate was 75%.

実施例 3 HBsAg陽性血漿を公知の方法で精製した逆受
身赤血球凝集反応(RPHA)で1:4000、比活
性はE280nm1:25000の純度のものを、等量
Freunds complete adjuvantと混合し、この0.1
mlずつを250〜300gのモルモツトの皮下又は皮内
に注射し、以後5週間0.1mlずつを同様追加免疫
して、その後抗HBs価を赤血球凝集法(PHA法)
で測定し、値の上がつた時点で全量の血液を採血
した。
Example 3 HBsAg positive plasma was purified by a known method using reverse passive hemagglutination (RPHA) with a purity of 1:4000 and a specific activity of E 280 nm of 1:25000.
This 0.1 mixed with Freunds complete adjuvant
Inject 250 to 300 g of guinea pigs subcutaneously or intradermally with 0.1 ml each for 5 weeks, and then measure the anti-HBs titer using the hemagglutination method (PHA method).
When the value rose, the entire amount of blood was collected.

以後実施例1の方式と同様の方法で精製し、酵
素処理した修飾抗HBs固定Sepharoseを得た。
Thereafter, the product was purified in the same manner as in Example 1 to obtain enzyme-treated modified anti-HBs-immobilized Sepharose.

本品1ml当たり、比活性としてE280nm当たり
RPHAで1:3000のHBsAgを、力価で1:
240000を吸着することが出来て、洗浄溶出後は比
活性としてE280nm当り1:32000以上で、回収率
96%以上を示した。
Per ml of this product, specific activity per E 280 nm
HBsAg at 1:3000 in RPHA and 1:3000 in titer.
240,000, and after washing and elution, the specific activity was more than 1:32,000 per E 280 nm, and the recovery rate was
It showed over 96%.

尚、酵素処理を行わない抗体による抗HBs固
定Sepharose 4Bでの精製では吸着率が劣り、と
りわけ比活性の上昇が、1:8000を上がらず、回
収率も75%程度を示した。
In addition, in purification using anti-HBs-immobilized Sepharose 4B using an antibody without enzyme treatment, the adsorption rate was poor, especially the increase in specific activity did not exceed 1:8000, and the recovery rate was about 75%.

実施例 4 公知の方法で精製した抗HBsモノクローナル
抗体のHAI法で1:1600000、比活性でE280nm当
たり1:55000の培養液を実施例1の方法で精製
し、抗HBs固定Sepharose 4Bを調製した。
Example 4 A culture solution of an anti-HBs monoclonal antibody purified by a known method using the HAI method with a specific activity of 1:55,000 per E 280 nm was purified using the method of Example 1, and anti-HBs-immobilized Sepharose 4B was purified using the HAI method. Prepared.

本品1ml当たり、比活性としてE280nm当たり
1:3000のHBsAgを力価で1:300000を吸着す
ることが出来て、洗浄溶出後は比活性として
E280nm当たり1:35000以上で、回収率95%以上
を示した。
1ml of this product can adsorb HBsAg with a titer of 1:300000 per E 280 nm as a specific activity, and after washing and elution, the specific activity is 1:300000.
The recovery rate was 95% or more with an E of 1:35000 or more per 280 nm.

尚、酵素処理を行わない抗体による抗HBs固
定Sephaprse 4Bでの精製では吸着率が劣り、と
りわけ比活性の上昇が、1:12000を上がらず、
回収率も73%程度であつた。
In addition, in purification using anti-HBs-immobilized Sephaprse 4B using an antibody without enzyme treatment, the adsorption rate was poor, and in particular, the increase in specific activity did not exceed 1:12000.
The recovery rate was also around 73%.

Claims (1)

【特許請求の範囲】 1 ペプシン、トリプシン、プラスミンから選ば
れる少なくとも一の蛋白分解酵素、およびアミラ
ーゼ、アルギナーゼから選ばれる少なくとも一の
糖分解酵素にて処理された抗体を固定化した担体
を吸着体とすることを特徴とする、前記抗体に対
応する抗原物質の精製方法。 2 抗原物質がウロキナーゼ、又はB型肝炎表面
抗原(HBsAg)である特許請求の範囲第1項記
載の精製方法。
[Claims] 1. A carrier on which an antibody treated with at least one proteolytic enzyme selected from pepsin, trypsin, and plasmin and at least one glycolytic enzyme selected from amylase and arginase is immobilized is used as an adsorbent. A method for purifying an antigenic substance corresponding to the antibody, characterized in that: 2. The purification method according to claim 1, wherein the antigenic substance is urokinase or hepatitis B surface antigen (HBsAg).
JP58237636A 1983-12-15 1983-12-15 Method for purifying antigenic substance Granted JPS60130526A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58237636A JPS60130526A (en) 1983-12-15 1983-12-15 Method for purifying antigenic substance

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58237636A JPS60130526A (en) 1983-12-15 1983-12-15 Method for purifying antigenic substance

Publications (2)

Publication Number Publication Date
JPS60130526A JPS60130526A (en) 1985-07-12
JPH04634B2 true JPH04634B2 (en) 1992-01-08

Family

ID=17018259

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58237636A Granted JPS60130526A (en) 1983-12-15 1983-12-15 Method for purifying antigenic substance

Country Status (1)

Country Link
JP (1) JPS60130526A (en)

Also Published As

Publication number Publication date
JPS60130526A (en) 1985-07-12

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