JPS60130526A - Method for purifying antigenic substance - Google Patents

Method for purifying antigenic substance

Info

Publication number
JPS60130526A
JPS60130526A JP58237636A JP23763683A JPS60130526A JP S60130526 A JPS60130526 A JP S60130526A JP 58237636 A JP58237636 A JP 58237636A JP 23763683 A JP23763683 A JP 23763683A JP S60130526 A JPS60130526 A JP S60130526A
Authority
JP
Japan
Prior art keywords
antibody
antigenic substance
purified
enzyme
urokinase
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
JP58237636A
Other languages
Japanese (ja)
Other versions
JPH04634B2 (en
Inventor
Masakazu Tajima
田島 政和
Yatsuhiro Kamimura
上村 八尋
Hirobumi Arimura
有村 博文
Masayuki Nishida
正行 西田
Takehiko Kawano
川野 武彦
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.)
Mitsubishi Tanabe Pharma Corp
Original Assignee
Green Cross Corp Japan
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 Japan filed Critical Green Cross Corp Japan
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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  • 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)
  • Enzymes And Modification Thereof (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

PURPOSE:To obtain an antigenic substance corresponding to an immunological antibody in high purity and recovery, by treating the immunological antibody haing a specificity for the antigenic substance to be purified to give a modified purified antibody having a high specificity, and immobilizing the resultant antibody in an insoluble carrier. CONSTITUTION:An immunological antibody, e.g. blood plasma or serum of an immunized animal or monoclonal antibody, having specificity for an antigenic substance to be purified, e.g. urokinase, HBsAg, kallikrein or interferon, is treated with an enzyme. Pepsin, trypsin, amylase, arginase, plasmin, etc. are preferably used as the enzyme. The resultant antibody is then immonilized in an insoluble carrier, e.g. purified agar gel, cellulosic derivative, dextran polymer or glass particles, etc., and the aimed antigenic substance is obtained in high purity and recovery from crude antigenic substance with the immobilized carrier having a high affinity therefor.

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
フィニティクロマトグラフィーを使用する、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. For more details,
The present invention uses the mechanisms of antigens and antibodies to enzyme-treat immune antibodies specific to the antigen substance to be purified, thereby producing modified purified antibodies with extremely high specificity.
The present invention relates to a method for producing an antigenic substance with high purity and high recovery rate from a crude antigenic substance 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。従って
、これを人体へ注射することにより血管内に生じた血栓
を熔解するので、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、その有用性が広がっている。
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 have formed in blood vessels, so it is not only effective in treating cerebral thrombosis and other thrombosis, but also increases the therapeutic effect when used in combination with anticancer drugs, making 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、ハイツロ
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。
Conventionally, urokinase purification has been carried out using silica gel, HytuloSupercell, zeolite acrylonitrile, barium sulfate, or various ion exchangers and gel filtration, as well as immunoadsorbents immobilized with anti-urokinase antibodies using the corresponding antibodies. ing.

また、B型肝炎表面抗原(HBsAg)も高純度化し、
不活化処理を行ったものはB型肝炎ワクチンとして利用
できる。
In addition, hepatitis B surface antigen (HBsAg) has been highly purified,
The inactivated vaccine can be 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。
As a method for purifying HBsAg, ammonium sulfate, aerosil, ion exchange resin, gel filtration, ultracentrifugation, and a method using an immunoadsorbent on which an anti-HBsAg antibody is immobilized using the corresponding antibody are used.

そこで本発明者等は、これら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 of the known purification methods, are easy to operate, and are 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 an anion exchanger, these impurities such as contaminant proteins and sugars cannot be cleaved. , cannot be disassembled.

ところが、抗体を適当な条件下、酵素にて処理すれば、
これら不純物を除去することができ、しかもかかる処理
抗体をアフィニティクロマトグラフィーにおける吸着体
のリガンドとし、当該抗体に対応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, if antibodies are treated with enzymes under appropriate conditions,
If these impurities can be removed and the treated antibody is used as a ligand for an adsorbent in affinity chromatography and used to purify the antigenic substance corresponding to the antibody, the antigenic substance can be recovered in high yield and purity. I discovered that.

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、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 relates to a method for purifying an antigenic substance corresponding to an antibody by using a carrier on which an enzyme-treated antibody is immobilized as an adsorbent.

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,
Moreover, in addition to being easy to operate, it is possible to improve the functionality of the insoluble carrier on which the immune antibody is immobilized and the biological stability (prevention of spoilage, generation of pyrogenic substances, etc.) during large-scale production.

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、抗体を生成しうるちのであれ
ばよく、たとえばウロキナーゼ、HBSAg、カリクレ
イン、インターフェロンなどがあげられる。
There are no particular limitations on the antigenic substance to be purified in the present invention, as long as it can be used to immunize animals to produce antibodies, such as urokinase, 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、酵素処理に付す際には、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、血清などであっ
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としては、蛋白分解酵素、あ
るいは糖分解酵素であり、たとえばペプシン、トリプシ
ン、アミラーゼ、アルギナーゼ、プラスミンなどが好適
に用いられる。2−れら酵素の1種または2種以上にて
処理すればよい。
The enzyme used for the enzyme treatment is a proteolytic enzyme or a glycolytic enzyme, such as pepsin, trypsin, amylase, arginase, and plasmin. 2-It may be treated with one or more of these enzymes.

酵素処理は個々の水通条件下で行われ、その条件は、た
とえば次の通りである。
Enzyme treatment is carried out under individual water passage conditions, for example as follows.

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、9112〜3.5
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p115
.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, in the case of pepsin, trypsin, and plasmin, 0.1 μg to 1 mg of antibody depending on the antibody purity.
.. 9112-3.5 using 1-100 μg/ml
p115 for 10 to 30 hours at 25 to 37°C, using 0.1 μg to 100 μg of β-amylase.
.. 5 to 8.5, and treated at 25 to 37°C for 10 to 30 hours. In the case of arginase, add 0.1 μg to 100 μg, and treat at pH 7.5 to 10 for 10 to 30 hours at 25 to 37°C.
Process time.

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って、E 280 n
 m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, the E 280 n is generally concentrated by dialysis, concentration and/or ultrafiltration and gel filtration.
The areas with high m are measured by the HAI method of anti-urokinase using the hemagglutination reaction method and pooled.

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。
As a carrier for immobilizing the antibody thus obtained, any conventionally known immobilization carrier can be suitably used.

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。
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[Cu −a
 trecasas らの方法CP、 Cuatrec
asas、 J、 Biol。
The antibody can be immobilized on a carrier by a conventionally known method [Cu-a
Method CP of trecasas et al., Cuatrec
asas, J., Biol.

Chem、、 245.3059 (1970) )〕
、またはこれに準する方法にて行えばよい。
Chem, 245.3059 (1970)]
, or a similar method.

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は、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%.
% - its specificity is very good,
When using a polymeric urokinase antibody, 100%
A similar high molecular weight 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 also 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、80.0
00II位/E290nm以上のものの、10〜20万
単位/mlとFreunds complete ad
juvantを均等混合する。
Example 1 Specific activity of urokinase purified by a known method, 80.0
00II/E290nm or higher, 100,000 to 200,000 units/ml and Freunds complete ad
Mix the juvant evenly.

この1mlを3〜4Kgの家兎に皮下、または皮肉注射
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(H
AI法)で測定し値の上がった時点で家兎の耳静脈より
1回に50m1ずつ採血した。
This 1 ml was injected subcutaneously or subcutaneously into a 3-4 kg domestic rabbit, followed by booster immunization with 0.5 ml every 4-6 weeks, and then the anti-urokinase titer was determined by hemagglutination method (H
When the value increased, 50 ml of blood was collected from the ear vein of the rabbit at a time.

コノ抗血vr4100IIllニ、まず硫安12gを加
え、その遠心上を青へpH7,2にて13gを追加して
沈お物を遠心分離で得た。
First, 12 g of ammonium sulfate was added to the anti-blood solution vr4100 II, and then 13 g was added to the centrifuged tube at pH 7.2, and the precipitate was obtained by centrifugation.

この沈載物をO,03M食塩を含む0.04Mリン酸緩
iti液のpH8,Oに82Bon mの吸光度で2付
近まで溶解した。
This precipitate was dissolved in a 0.04 M phosphoric acid solution containing 0.03 M common salt, pH 8.0, to an absorbance of around 2.0 at an absorbance of 82 Bon m.

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70m1(直径3cm、高さ1゜口)カラム
を通過して、抗ウロキナーゼ部分をHAl法とE29Q
nmで測定して、高純度抗ウロキナーゼ画分、約1gを
得た。
Then, this solution was equilibrated with the same buffer and DEAE-
Cellulose was passed through a 70 ml column (3 cm in diameter, 1° in height) and the anti-urokinase moiety was extracted using the HAl method and E29Q.
Approximately 1 g of a highly purified anti-urokinase fraction was obtained as determined by nm.

この抗ウロキナーゼ画分の40mg当たり、pH2゜5
にてペプシン1μg/終濃度として37°Cで18時間
の反応を行い、次いでlN−NaOHでpH6,5に調
製後、β−アミラーゼを5μg/終濃度ニシテ、25℃
で12時間処理して、最後にpi(9゜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pHloで1時間放置して、0.3M食塩
加0.(11M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七フアクリル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, pH 2.5
The reaction was carried out at 37°C for 18 hours at 1 μg/final concentration of pepsin, and then the pH was adjusted to 6.5 with 1N-NaOH, and then β-amylase was added at 5 μg/final concentration at 25°C.
Finally, 1 μg/final concentration of arginase was added at 9°2, treated for 18 hours at 25°C, and then left at room temperature for 1 hour in pHlo. 0. (dialyzed and concentrated with 11M phosphate buffer pH 8.5, gel-filtered with heptaphryl S-500 in the same buffer, and obtained approximately 0.4 g as an anti-urokinase fraction using the PHA method) I got it.

この酵素処理液のB 290 n mを、5付近に0.
1゜M炭酸ソーダ緩衝液pl+9で希釈して、はぼ等量
のCNBr−activated 5epharose
 4B (ファルアシア製)を加えて、4℃で24時間
ゆっくりと攪拌した。
The B 290 nm of this enzyme-treated solution was set to around 5 and 0.
Approximately equal amounts of CNBr-activated 5epharose were diluted with 1°M sodium carbonate buffer pl+9.
4B (manufactured by Falcia) was added, and the mixture was slowly stirred at 4°C for 24 hours.

この間、最初のHAI値は、1 : 2,000から1
=2付近に混合液は低下し、カップリングが順調に進ん
だことが判った。
During this period, the initial HAI value changed from 1:2,000 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ホウ酸緩術液
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5epharose 4Bを得た。
After the reaction was completed, it was thoroughly washed with a 0.15M salt-added 0.02M boric acid laxative solution pH 8 to obtain enzyme-treated modified anti-urokinase-immobilized 5epharose 4B.

本品1ml当たり、比活性3,000単位/ E 2B
0 nmの粗製ウロキナーゼは約300,000単位を
吸着することが出来て、同一緩衝液で洗浄後、0.5 
M食塩加0.17Mグリシンm tMj液にて溶出して
、比活性85,000単位/ E 2go n m以上
、回収率95%以上を得た。
Specific activity 3,000 units/E 2B per 1ml of this product
0 nm crude urokinase can adsorb approximately 300,000 units, and after washing with the same buffer, 0.5
Elution was performed with a 0.17M glycine m tMj solution containing M sodium chloride, and a specific activity of 85,000 units/E 2 go nm or more and a recovery rate of 95% or more were obtained.

同様に、比活性i 、 ooo単位/ E 280 n
 mの組織培養ウロキナーゼも約200,000単位が
吸着し、比活性100.000単位/E2B6nmで、
回収率95%以上を得た。
Similarly, specific activity i, ooo units/E 280 n
About 200,000 units of tissue culture urokinase of m were also adsorbed, and the specific activity was 100,000 units/E2B6nm.
A recovery rate of 95% or more was obtained.

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5epharose 4Bでの精製では吸着率が劣り
、とりわけ比活性の上昇が50,000単位/E2QO
nmを上がらず、回収率80%程度を示した。
In addition, purification using anti-urokinase-immobilized 5epharose 4B using an antibody without enzyme treatment resulted in poor adsorption rate, and in particular, the increase in specific activity was 50,000 units/E2QO.
The recovery rate did not exceed 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5epharose 4Bを用いて、本品11
111当たり、組織培養ウロキナーゼの培養液の約10
.000単位を吸着することが出来て、比活性として9
0,000単位/E2gQnm以上のものを回収率95
%で得た; 尚、酵素処理を行わない抗体による抗ウロキナーゼ固定
5epharose 4Bでの精製では吸着率が劣り、
とりわけ比活性の上昇が75.000単位/ E 2o
Example 2 Using the enzyme-treated modified anti-urokinase immobilized 5epharose 4B prepared in Example 1, this product 11
Approximately 10 per 111 of culture medium of tissue culture urokinase
.. 000 units and has a specific activity of 9.
Recovery rate of 0,000 units/E2gQnm or more is 95
%; Note that purification using anti-urokinase-immobilized 5epharose 4B using antibodies without enzyme treatment resulted in poor adsorption;
In particular, the increase in specific activity was 75,000 units/E2o
.

nmで回収率が75%を示した。The recovery rate was 75% at nm.

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(RP HA)で1:4,000、比活性は
E 286 n m l : 250,000の純度の
ものを、等量Freunds complete ’a
djuvantと混合し1この0.1mlずつを250
〜300gのモルモットの皮下又は皮肉に注射し、以後
5週間0.1mlずつを同様追加免疫して、その後抗H
Bs価を赤血球凝集法(PHA法)で測定し、値の上が
っ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 (RP HA) with a purity of 1:4,000 and a specific activity of E 286 nml: 250,000, and an equal amount of Freunds complete 'a
Mix with djuvant and add 0.1ml of this to 250ml each.
~300 g of guinea pigs were injected subcutaneously or subcutaneously, and then boosted in the same manner with 0.1 ml for 5 weeks, followed by anti-H
Bs titer was measured by hemagglutination method (PHA method), and 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HB s固定5epharoseを得た。
Thereafter, it was purified in the same manner as in Example 1 to obtain enzyme-treated modified anti-HBs-immobilized 5epharose.

本品1ml当たり、比活性としてE 2Bo n m当
たりRP HAで1:3,000のHBSAgを、力価
で1 : 240,000を吸着することが出来て、洗
浄溶出後は比活性としてE 2Bo n m当たり1 
: 320,000以上で、回収率96%以上を示した
1 ml of this product can adsorb HBSAg with a specific activity of 1:3,000 in RP HA per m of E2Bo, and a titer of 1:240,000, and after washing and elution, the specific activity is E2Bo. 1 per nm
: 320,000 or more, indicating a recovery rate of 96% or more.

尚、酵素処理を行わない抗体による抗HB s固定5e
pl+arose 4Bでの精製では吸着率が劣り、と
りわけ比活性の上昇が、1:8,000を上がらず、回
収率も75%程度を示した。
In addition, anti-HBs immobilization 5e with antibody without enzyme treatment
In purification with pl+arose 4B, the adsorption rate was poor, especially the increase in specific activity did not exceed 1:8,000, 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17
1HAI法テ1 : 1,600,000 、比活性T
:Ez8゜nm当たりI : 55,000の培!#:
液を実施例1の方法で精製し、抗HB s固定5eph
arose 4Bを調製した。
Example 4 Anti-HBs monoclonal antibody 17 purified by a known method
1 HAI method Te 1: 1,600,000, specific activity T
:I per Ez8゜nm: 55,000 cultivation! #:
The solution was purified by the method of Example 1, and anti-HBs immobilized at 5eph.
arose 4B was prepared.

本品1ml当たり、比活性としてEzaon’m当たり
1 : 3,000 (7)HB s A gを力価テ
1 : 300,000を吸着することが出来て、洗浄
溶出後は比活性としてE2aOnm当たり1 : 35
,000以上で、回収率95%以上を示した。
1ml of this product can adsorb HBsA g with a titer of 1:300,000 per Ezaon'm as a specific activity, and after washing and elution, the specific activity is per E2aOnm. 1:35
,000 or more, indicating a recovery rate of 95% or more.

尚、酵素処理を行わない抗体による抗HBs固定5ep
l+arose 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 : 12.000を上がらず
、回収率も73%程度でおった。
In addition, anti-HBs fixation 5ep with antibody without enzyme treatment
In the purification using l+arose 4B, the adsorption rate was poor, especially the increase in specific activity did not exceed 1:12.000, and the recovery rate was about 73%.

特許出願人 株式会社 ミドリ十字 手続補正書印釦 昭和59年3月B日 1、事件の表示 ゛ 昭和58年特許願第237636号 2、発明の名称 抗原物質の精製方法 3、補正をする考 事件との関係 特許出願人 氏名(名称) 株式会社 ミトリ十字 4、代理人 ■541 住 所 大阪市東区平野町4丁目53番地3ニューライ
フ平野町406号 電話(06) 227−1156 6.1ili正の対象 明細書の「発明の詳に、Illな説明」の欄7、補正の
内容 (1)明細書第10頁、第14行のr 1 : 250
,000 Jをr ] : 25,0OOJに訂正する
Patent Applicant: Midori Juji Co., Ltd. Letter of amendment, stamped on March B, 1980, 1, Indication of the case: Patent Application No. 237636, filed in 1982, 2, Name of the invention: Method for purifying antigenic substances 3, Review case for amendment Relationship with Patent Applicant Name Mitri Juji Co., Ltd. 4, Agent ■541 Address 406 New Life Hirano-cho, 4-53-3 Hirano-cho, Higashi-ku, Osaka Phone: (06) 227-1156 6.1ili Masano Column 7 of “Detailed explanation of the invention” of the subject specification, contents of amendment (1) r 1 on page 10, line 14 of the specification: 250
,000 J to r]: Correct it to 25,0OOJ.

方式(i1°゛)゛・、1゛i・割:Method (i1°゛)゛・, 1゛i・discount:

Claims (1)

【特許請求の範囲】 fil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。 (3)酵素がペプシン、トリプシン、アミラーゼ、アル
ギナーゼ、プラスミンから選ばれる、少なくとも一種で
ある特許請求の範囲第fi1項または第(2)項記載の
精製方法。
[Scope of Claims] A method for purifying an antigenic substance corresponding to an antibody, characterized in that a carrier on which an antibody treated with a fil enzyme is immobilized is used as an adsorbent. (2) The purification method according to claim (1), wherein the antigenic substance is urokinase or hepatitis B surface antigen (HBSAg). (3) The purification method according to claim 1 or 2, wherein the enzyme is at least one selected from pepsin, trypsin, amylase, arginase, and plasmin.
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 true JPS60130526A (en) 1985-07-12
JPH04634B2 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
JPH04634B2 (en) 1992-01-08

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