JPS6363559B2 - - Google Patents

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Publication number
JPS6363559B2
JPS6363559B2 JP56209841A JP20984181A JPS6363559B2 JP S6363559 B2 JPS6363559 B2 JP S6363559B2 JP 56209841 A JP56209841 A JP 56209841A JP 20984181 A JP20984181 A JP 20984181A JP S6363559 B2 JPS6363559 B2 JP S6363559B2
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active substance
physiologically active
buffer
salt concentration
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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、制ガン作用を有する蛋白性生理活性
物質の精製方法に関するものである。 Carswell氏らは、あらかじめbacillus Calme
−tte−Gue′rin(BCG)を投与したCD−1
Swissマウスに2週間後にエンドトキシンを静脈
内注射して得られる該マウスの血清が、培養L
cellに対して殺細胞能を有すること及びMeth A
sarcomaで担癌させた(BALB/c×
C57BL/6)F1マウスの腫瘍を出血性壊死に至
らしめる現像を見出し、TNF(Tumor Necrosis
Factor)と名づけた〔Proc.Nat.Acad.Sci.
USA72巻(No.9)3666〜3670頁(1975年)〕。そ
の後彼らは、該血清からTNFの部分精製を行な
つた結果、原血清に比べて20〜30倍精製された活
性画分を得、その活性物質はセルロースアセテー
ト膜電気泳動でα−グロブリン分画に泳動される
分子量約150000の糖蛋白質であると報告した
〔Proc.Nat.Acad.Sci.USA73巻(No.2)381〜385
頁(1976年)〕。 Ma¨nnel氏らは、前記Carswell氏らの方法によ
つて得られたマウス血清を用いて抗腫瘍性因子
(Cytotoxic Factor)の性状を調べ、ゲル過に
用いる緩衝液中の塩濃度を変えることにより、活
性容出画分が変動することを見出し、高塩濃度緩
衝液中では分子量が55000〜60000、低塩濃度緩衝
液中または血清中では会合により分子量が125000
〜150000になることを報告した〔Infec.
Immun.28巻(No.1)204〜211頁(1980年)〕。し
かし、この因子の動物での評価(例えばMeth A
sarcoma担癌マウスを用いる評価)を行なつて
いず、その活性の有無は不明であり、Carswell
氏らのTNFと同一のものか否かは判断できない。
また彼らは、Lcellを用いる活性測定で各種の性
状を調べているものの精製方法については述べて
いない。 またMatthews氏らは、ウサギでTNFを誘発
させ、その血清を用いてウサギTNFの性状を調
べ、ウサギTNFの分子量はセフアデツクスG−
200を用いるゲル過法では40000〜50000の範囲
にあると報告した〔Br.J.Cancer38巻302〜309頁
(1978年)〕。 本発明者は、このような技術水準の下に、網内
系賦活化作用を有する物質を哺乳動物に投与し、
次いでエンドトキシンを注射することによつて、
又は哺乳動物由来の活性化マクロフアージを含む
組識倍養系にエンドトキシンを加えることによつ
て誘発される制ガン作用を有する生理活性物質の
実用的価値の高い精製方法を見出すべく鋭意研究
を重ねた結果、比較的高純度の該生理活性物質が
好収率で得られ、しかも大規模精製に適した簡便
な精製方法を見出した。 本発明は、網内系賦活化作用を有する物質の1
種又は2種以上を哺乳動物に投与し、次いでグラ
ム陰性菌由来のエンドトキシンを注射することに
よつて、又は哺乳動物由来の活性化マクロフアー
ジを含む組識倍養系にグラム陰性菌由来のエンド
トキシンを加えることによつて誘発される制ガン
作用を有する蛋白性生理活性物質の粗製溶液を、
(1)PH6.0〜9.0、塩濃度0.2M以下の緩衝液を用いて
塩基性陰イオン交換体と接触させて該生理活性物
質を吸着させ、(2)吸着時の塩濃度よりも高塩濃度
の緩衝液を用いて該吸着生理活性物質を該塩基性
陰イオン交換体から溶出させ、次いで(3)該生理活
性物質を含む溶出液を分子量30000〜70000の物質
の分離に適した担体及び溶出液としてPH6.0〜9.0
の緩衝液を用いるゲル過に付し、さらに必要に
応じて(4)該生理活性物質画分を下記の構造式 を有する固定化染料を用いるアフイニテイークロ
マトグラフイーに付すことを特徴とする、制ガン
作用を有する蛋白性生理活性物質の精製方法に関
するものである。 本発明に係る生理活性物質(以下、本生理活性
物質と記す。)を誘発させるためには、まず、
Carswell氏らの方法〔Proc.Nat.Acad.Sci・
USA72巻(No.9)3666〜3670頁(1975年)〕に準
じて、哺乳動物(例えばマウス、ウサギ、モルモ
ツト等)に網内系賦活化作用を有する物質の1種
又は2種以上を静脈内又は腹腔内に注射する。網
内系賦活化作用を有する物質としては、通常グラ
ム陽性菌、原生動物又は酵母が用いられ、生菌状
態、死菌状態(例えば熱処理がホルマリン処理
後)又は菌体抽出成分として投与される。ここ
で、グラム陽性菌としては、例えば
Propionibacteriumacnes(Corynebacterium
parvum)、Propioniba−cterium granulosum
(Corynebacterium granulo−sum)のような
Propionibacteria.bacillusCalmette−Gu−e′rin
(BCG)、Mycobacteriumsmegmatisのような
Mycobacteria.Nocardiaerythropolis、
Nocardia gardneriのようなNoca−rdiasが挙げ
られる。原生動物としては。例えばマラリア原
虫、トキソプラズマが挙げられる。酵母の場合、
通常Saccharomyces cerevisiaeなどから抽出し
たZymosanが用いられる。また、ピランコーポ
リマーのような合成高分子化合物を用いることも
できる。投与後7〜14日後にグラム陰性菌より得
られたエンドトキシン、例えば大腸菌、緑膿菌、
チフス由来のリポポリサツカライドを該哺乳動物
の静脈内に注射する。注射後1.5〜2時間後に、
該哺乳動物の体液(例えば腹水、リンパ液等)及
び/又は血清もしくは血漿を得、また該動物の肝
臓、脾臓等の臓器を均一に破砂し、生理食塩水で
抽出する。これらの体液、血清、血漿及び/又は
臓器抽出液が本生理活性物質の粗製溶液として用
いられるが、通常は血清又は血漿が用いられる。 本生理活性物質を誘発させる他の方法は、哺乳
動物由来の活性化マクロフアージを含む組識倍養
系にエンドトキシンを加えることにより行なわれ
る。例えば、網内系賦活化作用を有する物質の1
種又は2種以上を投与した哺乳動物から、腹腔浸
出液、稗臓、又は肝臓由来の活性化マクロフアー
ジを常法により採取し、その組識倍養系にエンド
トキシンを加えると、上清中に本生理活性物質が
遊離する。この上清もまた、本生理活性物質の粗
製溶液として用いられる。 本生理活性物質の生理活性評価は以下の方法に
より行なう。 (a) L cellを用いる評価: Carswell氏らの方法〔Proc.Nat.Acad.Sci・
USA72巻(No.9)3666〜3670頁(1975年)〕に
準じて行なう。 培養容器としてリンブロ社製(米国)のプレ
ートを使用し、非必須アミノ酸及び10%の熱不
活化牛胎児血清、さらにペニシリン100単位/
ml、ストレプトマイシン100μg/mlを含むイ
ーグルの最小必須培地(MEM培地)とLcell
(S)を用いて行なう。細胞懸濁液(1×105
細胞)及び同容量の希釈試料を5%炭酸ガス含
有空気中、37℃で48時間培養する。力価は、試
料の希釈度とL cellの生存細胞をグラムにプ
ロツトし、L cellの50%殺細胞能に対応する
希釈度から算出する。L cellの50%を殺すた
めに必要な生理活性量を1単位とする。 (b) Meth A sarcoma担癌マウスを用いる評
価: Carswell氏らの方法(同上文献)に準じ、
(BALB/c×C57BL/6)F1マウスの腋下部
皮内に2×105のMeth A sarcoma細胞を移
植し、7日後、移植した腫瘍の大きさが直径7
〜8mmとなり、出血性壊死等がなく良好な血行
状態いあるマウスに、尾静脈より生理食塩水で
希釈した試料の0.5mlを注射し、24時間後に次
の判定基準に則り判定する。 (−):変化なし (+):かすかな出血性壊死 ():中程度の出血性壊死(移植癌表面の真中
から50%以上にわたつて壊死 ():顕著な出血性壊死(移植癌の中央部が重
度に壊死し、周囲の癌組識がわずかに残つた状
態) 以下に、本発明の精製方法の詳細を説明する。
第1工程である塩基性陰イオン交換体との接触に
先立ち、粗製溶液を陰イオン交換体との接触時に
用いる緩衝液に対して透析してもよいし、又は低
塩濃度の緩衝液で希釈してもよい。 粗製溶液と塩基性陰イオン交換体との接触は、
カラム法、バツチ法のいずれで行なつてもよい。
本工程は、粗製溶液をPH6.0〜9.0、塩濃度0.2M以
下の緩衝液を用いて塩基性陰イオン交換体に接触
させて本生理活性物質を吸着させ、次いで同緩衝
液で該イオン交換体を洗浄して非吸着蛋白質を除
去した後、高塩濃度の緩衝液を用いて本生理活性
物質を溶出させることにより行なわれる。 塩基性陰イオン交換体の具体例としては、
DEAE−セフアデツクスA−50、DEAE−セフア
ロースCL−6B、DEAE−セフアセル(以上フア
ルマシア社製、スウエーデン)AIEC DE52(ワツ
トマン社製、英国)のようなジエチルアミノ基含
有陰イオン交換体、Servacel AE(セルバ社製、
西独)のようなアミノエチル基含有陰イオン交換
体、QAE−セフアデツクスA−50(フアルマシア
社製)、CellexQAE(バイオーラツド社製、米国)
のような四級化アミノエチル基含有陰イオン交換
体等が挙げられる。緩衝液としては。例えば希薄
なトリス−塩酸緩衝液及びリン酸緩衝液が挙げら
れる。塩濃度を調節するために加える塩として
は、塩化ナトリウム、塩化カリウムが好ましい。
溶出液中の蛋白質濃度は、280nmに於ける吸光
度で測定され、本生理活性物質の濃度は前記した
L cell殺細胞力価として測定される。 陰イオン交換体との接触は一度で充分である
が、カラム法では再クロマトグラフイーが好まし
い場合がある。 前記工程で得られた本生理活性物質を含む溶出
液は、限外過、凍結乾燥等の常法で濃縮した
後、分子量30000〜70000の物質の分離に適した担
体を用いるゲル過に付す。溶出液としては緩衝
液が用いられ、そのPHは通常6.0〜9.0である。緩
衝液中の塩濃度は、粗製溶液としてマウス血清又
は血漿を用いる場合には、0.5M以上、好ましく
は0.7〜2.0Mである。他の動物種の血清又は血漿
を用いる場合には、特に限定されないが、好まし
くは0.15〜2.0Mである。ゲル過用担体の具体
例としては、セフアデツクスG−75、100、150、
200(フアルマシア社製)、セフアクリルS−200、
300(フアルマシア社製)、Bio−GelP−30、60、
100、150、200(バイオーラツド社製)、CPG−
100(350Å、240Å、170Å、120Å)(エレクトロ
ーヌクレオニクス社製、米国)、等が挙げられる。
緩衝液及び加えられる塩としては、前記工程で挙
げたものが同様に用いられる。 ゲル過で得た、本生理活性物質を含有する画
分を集め、限外過、凍結乾燥等の常法で濃縮
し、生理食塩水に対して透析すると、動物種によ
つて異なるが、原血清又は原血漿に比べて約200
〜10000倍精製された溶液が得られ、二工程を通
してのL cellを用いる評価による活性回収率は
約50〜100%である。さらに、精製を必要とする
場合には、先に得た濃縮液をシバクロンブルー
F3G−A(チバガイギー社製)を固定した担体を
用いるアフイニテイークロマトグラフイーに付
す。 シバクロンブルーF3G−A(染料)の担体固定
化及び不溶化は、公知の方法〔例えばBo¨hme氏
らの方法、J.Chromatogr.69巻209〜214頁(1972
年)〕に従つて行なつてもよいし、市販の固定化
担体〔例えばブルーセフアロースCL−6B(フア
ルマシア社製)、アフイーゲルブルー(バイオー
ラツド社製)〕を用いてもよい。本生理活性物質
の濃縮液をPH7.0〜8.0の希薄な緩衝液(例えばリ
ン酸緩衝液、トリス−塩酸緩衝液)に対して透析
した後、上記シバクロンブルーF3G−A固定化担
体に付す。この操作により夾雑蛋白質であるアル
ブミン等が吸着され、本生理活性物質は非吸着画
分に溶出される。この溶出液の精製度は原血清又
は原血漿に比べて約1000〜30000倍であり、三工
程を通しての活性回収率は約43〜95%である。 このようにして得られた本生理活性物質の精製
溶液を透析又はゲル過によりPH及び塩濃度を調
整し、過滅菌し、必要ならば加熱処理後、凍結
乾燥することにより、本生理活性物質の精製物を
得ることができる。ここの精製物約3000単位は、
前記したMeth Asarcoma担癌マウスを用いる評
価に於いて(−)の活性を示した。本生理活性物
質の精製物は各種培養ヒト癌細胞に対しても殺細
胞作用を示した。精製物800単位の48時間後に於
ける殺細胞率を表1に示す。
The present invention relates to a method for purifying a proteinaceous physiologically active substance having anticancer activity. Mr. Carswell et al.
-tte-Gue′rin (BCG) administered CD-1
The serum of Swiss mice obtained by intravenous injection of endotoxin after 2 weeks was cultured in L.
Having cytocidal ability against cells and Meth A
Tumor was loaded with sarcoma (BALB/c×
We discovered that tumors in C57BL/6) F 1 mice developed into hemorrhagic necrosis.
Factor) [Proc.Nat.Acad.Sci.
USA Vol. 72 (No. 9) pp. 3666-3670 (1975)]. They then partially purified TNF from the serum and obtained an active fraction that was 20 to 30 times more purified than the original serum, and the active substance was separated into α-globulin fractions by cellulose acetate membrane electrophoresis. [Proc.Nat.Acad.Sci.USA Vol. 73 (No. 2) 381-385]
Page (1976)]. Ma¨nnel et al. investigated the properties of antitumor factors (cytotoxic factors) using mouse serum obtained by the method of Carswell et al. It was discovered that the active volume fraction fluctuates, and the molecular weight is 55,000-60,000 in high-salt buffers, and 125,000 in low-salt buffers or serum due to association.
~150,000 [Infec.
Immun. vol. 28 (No. 1) pp. 204-211 (1980)]. However, evaluation of this factor in animals (e.g. Meth A
Carswell
It cannot be determined whether it is the same as the TNF reported by et al.
Furthermore, although they investigated various properties by measuring activity using Lcell, they did not describe the purification method. In addition, Matthews et al. induced TNF in rabbits, investigated the properties of rabbit TNF using the serum, and determined that the molecular weight of rabbit TNF was
It was reported that the gel filtration method using 200 was in the range of 40,000 to 50,000 [Br.J.Cancer Vol. 38, pp. 302-309 (1978)]. Based on the above-mentioned state of the art, the present inventor administered a substance having a reticuloendothelial system activating effect to a mammal,
Then by injecting endotoxin,
We also conducted intensive research to find a highly practical method for purifying physiologically active substances with anticancer effects induced by adding endotoxin to a tissue culture system containing activated macrophages derived from mammals. As a result, we have found a simple purification method that allows the physiologically active substance to be obtained with relatively high purity in good yield and is suitable for large-scale purification. The present invention provides one of the substances having reticuloendothelial system activation effect.
endotoxin from Gram-negative bacteria by administering the species or species to a mammal and then injecting endotoxin from Gram-negative bacteria or into a tissue culture system containing activated macrophages from mammals. A crude solution of a proteinaceous physiologically active substance that has an anticancer effect induced by adding
(1) Adsorb the physiologically active substance by contacting it with a basic anion exchanger using a buffer solution with a pH of 6.0 to 9.0 and a salt concentration of 0.2M or less, and (2) a salt concentration higher than that at the time of adsorption. The adsorbed physiologically active substance is eluted from the basic anion exchanger using a buffer solution with a concentration of PH6.0~9.0 as eluent
The physiologically active substance fraction is subjected to gel filtration using a buffer solution of (4) as required. The present invention relates to a method for purifying a proteinaceous physiologically active substance having an anticancer effect, which is characterized by subjecting it to affinity chromatography using an immobilized dye having an anticancer effect. In order to induce the physiologically active substance according to the present invention (hereinafter referred to as the present physiologically active substance), first,
Carswell et al.'s method [Proc.Nat.Acad.Sci・
USA Vol. 72 (No. 9) pp. 3666-3670 (1975)], mammals (e.g., mice, rabbits, guinea pigs, etc.) are given one or more substances that activate the reticuloendothelial system intravenously. Inject intravenously or intraperitoneally. Gram-positive bacteria, protozoa, or yeast are usually used as the substance having a reticuloendothelial system activation effect, and are administered in a live state, a dead state (for example, after heat treatment with formalin), or as a bacterial cell extract component. Here, as Gram-positive bacteria, for example,
Propionibacterium acnes (Corynebacterium
parvum), Propioniba-cterium granulosum
(Corynebacterium granulo−sum)
Propionibacteria.bacillus Calmette−Gu−e′rin
(BCG), Mycobacterium smegmatis-like
Mycobacteria.Nocardiaerythropolis,
Examples include Noca-rdias such as Nocardia gardneri. As a protozoan. Examples include malaria parasites and Toxoplasma gondii. In the case of yeast,
Zymosan extracted from Saccharomyces cerevisiae etc. is usually used. Moreover, synthetic polymer compounds such as pyran copolymers can also be used. Endotoxin obtained from Gram-negative bacteria 7 to 14 days after administration, such as Escherichia coli, Pseudomonas aeruginosa,
Typhoid-derived lipopolysaccharide is injected intravenously into the mammal. 1.5 to 2 hours after injection,
Body fluids (eg, ascites, lymph fluid, etc.) and/or serum or plasma of the mammal are obtained, and organs such as the liver and spleen of the animal are homogeneously crushed and extracted with physiological saline. These body fluids, serum, plasma, and/or organ extracts are used as crude solutions of the physiologically active substance, and usually serum or plasma is used. Another method of inducing this physiologically active substance is by adding endotoxin to a tissue culture system containing activated macrophages of mammalian origin. For example, one of the substances that has the effect of activating the reticuloendothelial system.
Activated macrophages derived from peritoneal exudate, glenoid, or liver are collected from mammals to which the species or two or more species have been administered, and endotoxin is added to the tissue culture system. The active substance is liberated. This supernatant is also used as a crude solution of the physiologically active substance. The physiological activity of this physiologically active substance is evaluated by the following method. (a) Evaluation using L cell: Carswell et al.'s method [Proc.Nat.Acad.Sci.
USA Vol. 72 (No. 9) pp. 3666-3670 (1975)]. A plate made by Linbro (USA) was used as a culture vessel, and non-essential amino acids, 10% heat-inactivated fetal bovine serum, and 100 units of penicillin were added.
ml, Eagle's minimum essential medium (MEM medium) containing streptomycin 100 μg/ml and Lcell
(S). The cell suspension (1×10 5 cells) and the same volume of diluted sample are cultured at 37° C. for 48 hours in air containing 5% carbon dioxide. The titer is calculated by plotting the dilution of the sample and the viable cells of L cells in grams, and then calculating the dilution corresponding to 50% cell-killing ability of L cells. One unit is the amount of physiological activity required to kill 50% of L cells. (b) Evaluation using Meth A sarcoma tumor-bearing mice: According to the method of Carswell et al. (ibid.)
(BALB/c×C57BL/6) 2×10 5 Meth A sarcoma cells were implanted intradermally in the axillary region of F 1 mice, and after 7 days, the size of the implanted tumor was 7 in diameter.
0.5 ml of the sample diluted with physiological saline was injected into the tail vein of a mouse with a size of ~8 mm and good blood circulation without hemorrhagic necrosis, and after 24 hours it was judged according to the following criteria. (-): No change (+): Faint hemorrhagic necrosis (): Moderate hemorrhagic necrosis (necrosis extending from the center of the transplanted cancer surface to more than 50% (): Significant hemorrhagic necrosis (necrosis of the transplanted cancer) The central part is severely necrotic, with only a small amount of surrounding cancer tissue remaining) The details of the purification method of the present invention will be explained below.
Prior to the first step, contacting with the basic anion exchanger, the crude solution may be dialyzed against the buffer used during contact with the anion exchanger or diluted with a low salt buffer. You may. The contact of the crude solution with the basic anion exchanger is
Either a column method or a batch method may be used.
In this step, the crude solution is brought into contact with a basic anion exchanger using a buffer solution with a pH of 6.0 to 9.0 and a salt concentration of 0.2M or less to adsorb the physiologically active substance, and then the ion exchanger is used with the same buffer solution. This is done by washing the body to remove unadsorbed proteins, and then eluting the physiologically active substance using a buffer with a high salt concentration. Specific examples of basic anion exchangers include:
Diethylamino group-containing anion exchangers such as DEAE-Sephadex A-50, DEAE-Sepharose CL-6B, DEAE-Sephacel (manufactured by Pharmacia, Sweden), AIEC DE52 (manufactured by Watmann, UK), Servacel AE (manufactured by Serva, Sweden), Made by
Aminoethyl group-containing anion exchangers such as (West Germany), QAE-Sephadex A-50 (manufactured by Pharmacia), CellexQAE (manufactured by Biorad, USA)
Examples include quaternized aminoethyl group-containing anion exchangers such as. As a buffer solution. Examples include dilute Tris-HCl buffer and phosphate buffer. The salt added to adjust the salt concentration is preferably sodium chloride or potassium chloride.
The protein concentration in the eluate is measured by absorbance at 280 nm, and the concentration of the physiologically active substance is measured as the L cell killing titer described above. Although one contact with the anion exchanger is sufficient, rechromatography may be preferred in column methods. The eluate containing the physiologically active substance obtained in the above step is concentrated by a conventional method such as ultrafiltration or freeze drying, and then subjected to gel filtration using a carrier suitable for separating substances with a molecular weight of 30,000 to 70,000. A buffer is used as the eluent, and its pH is usually 6.0 to 9.0. The salt concentration in the buffer is 0.5M or more, preferably 0.7 to 2.0M when mouse serum or plasma is used as the crude solution. When using serum or plasma of other animal species, the concentration is preferably 0.15 to 2.0M, although it is not particularly limited. Specific examples of carriers for gel filtration include Cephadex G-75, 100, 150,
200 (manufactured by Pharmacia), Sefacrylic S-200,
300 (manufactured by Pharmacia), Bio-GelP-30, 60,
100, 150, 200 (manufactured by Biorad), CPG-
100 (350 Å, 240 Å, 170 Å, 120 Å) (manufactured by Electronucleonics, USA), and the like.
As the buffer solution and the salt to be added, those listed in the above steps can be used in the same manner. The fractions containing this physiologically active substance obtained by gel filtration are collected, concentrated using conventional methods such as ultrafiltration and freeze-drying, and dialyzed against physiological saline. Approximately 200% compared to serum or original plasma
A ~10,000-fold purified solution is obtained, and the activity recovery rate evaluated using L cell through two steps is approximately 50-100%. Furthermore, if purification is required, use Cibacron Blue as the concentrate obtained earlier.
It is subjected to affinity chromatography using a carrier fixed with F3G-A (manufactured by Ciba Geigy). Cibacron Blue F3G-A (dye) is immobilized on a carrier and insolubilized using known methods [for example, the method of Bo¨hme et al., J. Chromatogr. 69, pp. 209-214 (1972
)], or commercially available immobilization carriers [for example, Blue Sepharose CL-6B (manufactured by Pharmacia), Afui Gel Blue (manufactured by Biorad)] may be used. After dialyzing the concentrated solution of this physiologically active substance against a dilute buffer solution with a pH of 7.0 to 8.0 (e.g., phosphate buffer, Tris-HCl buffer), it is applied to the Cibacron Blue F3G-A immobilization carrier. . Through this operation, contaminant proteins such as albumin are adsorbed, and the physiologically active substance is eluted in the non-adsorbed fraction. The degree of purification of this eluate is approximately 1,000 to 30,000 times higher than that of original serum or plasma, and the activity recovery rate through the three steps is approximately 43 to 95%. The purified solution of the physiologically active substance obtained in this way is subjected to dialysis or gel filtration to adjust the pH and salt concentration, is over-sterilized, and if necessary is heated and then freeze-dried to produce the physiologically active substance. A purified product can be obtained. Approximately 3000 units of refined products here are
In the evaluation using Meth Asarcoma tumor-bearing mice described above, it showed (-) activity. The purified product of this physiologically active substance also showed cytocidal activity against various cultured human cancer cells. Table 1 shows the cell killing rate of 800 units of the purified product after 48 hours.

【表】 一方、ヒト及びマウス培養線維芽細胞などの正
常細胞に対しては、本生理活性物質の精製物は、
2×106の単位でも殺細胞作用を示さなかつた。 さらに、結腸癌Colon26で担癌させたBALB/
cマウス及び神径芽細胞腫Neuro−2aで担癌させ
たA/Jaxマウスに本生理活性物質の精製物を投
与した試験に於いて、対照群(生理食塩水投与
群)に比して有意な癌の増殖抑制と退縮が認めら
れた。なお、個体によつては出血性壊死を起こさ
ずに定着癌が退縮・消失する場合があつた。 本生理活性物質の精製物は、極めて優れた制ガ
ン作用を有し、その作用は種特異性が少ないの
で、極めて有用な抗腫瘍剤として期待できるもの
である。 以下に実施例を示して本発明をよい具体的に述
べるが、本発明はこれら実施例に限定されるもの
ではない。 実施例 1 雌ウサギ(体重2.5〜3Kg)にホルマリンにて
死菌処理したPropionibacterium acnes(Coryne
−bacterium parvum;ウエルカム社、英国)50
mgを耳静脈により注射した。該ウサギに8日後再
度100μgのエンドトキシン(水腸菌026:B6)由
来のリポポリサツカライド、デイフコ社製、米
国)を耳静脈より注射し、2時間後に心臓により
全採血した。採取した血液は5000rpmで30分間遠
心操作を行ない、血球及び不溶固形物を除去し
た。20羽のウサギより12800単位/mlの力価を有
する血清1200mlが得られた。 該血清を600mlの0.02Mトリス−塩酸緩衝液
(PH7.8)で希釈後、0.1Mの塩化ナトリウムを含
む0.02Mトリス−塩酸緩衝液(PH7.8)であらか
じめ平衡化したDEAE−セフアロースCL−6B
(フアルマシア社製)のカラム(6×36cm)に、
徐々に付した。次いで1000mlのカラム平衡化緩衝
液(0.1M塩化ナトリウムを含む0.02Mトリス−
塩酸緩衝液、PH7.8)で洗浄した後、1.5の0.1M
塩化ナトリウムを含む0.02Mトリス−塩酸緩衝液
(PH7.8)と1.5の0.3M塩化ナトリウムを含む
0.02Mトリス−塩酸緩衝液(PH7.8)とを用いて、
グラジエンターによる塩化ナトリウム直線塩濃度
勾配によつて溶出を行なつた。流速60ml/時の条
件で18mlずつ分画して活性画分を採取し、濃縮し
た。この段階での活性回収率は92%、精製度は原
血清の150倍であつた。 次いで、該濃縮液を0.15M塩化ナトリウムを含
む0.005Mリン酸緩衝液(PH7.4)に一液透析後、
ゲル過を行なつた。セフアクリルS−200(フア
ルマシア社製)のカラム(5×80cm)を用い、同
緩衝液で充分平衡化した後、該濃縮液を付し、同
緩衝液にてゲル過溶出を行なつた。流速60ml/
時で10mlずつ分画して活性画分を採取した。アル
ブミン画分の直後に得られた活性画分を限外過
により濃縮して、本生理活性物質の精製物を得
た。この段階では、活性回収率92%、精製度52倍
であり、全段階を通しては活性回収率85%、精製
度7800倍であつた。なお本生理活性物質の精製物
の比活性は約1.4×106単位/mg蛋白質であつた。 第1図及び第2図にそれぞれDEAE−セフアロ
ースCL−6Bカラムでのクロマトグラフイー(第
1工程)及びセフアクリルS−200カラムでのゲ
ル過(第2工程)のパターンを示す。 実施例 2 本生理活性物質を含有するウサギ血清2200mlを
0.02トリス−塩酸緩衝液(PH7.2)1200mlで希釈
した後、0.1Mの塩化ナトリウムを含む0.02Mト
リス−塩酸緩衝液(PH7.2)であらかじめ平衡化
したDEAE−セフアロースCL−6Bのカラム(8
×26cm)に、徐々に付した。次いで、0.13Mの塩
化ナトリウムを含む0.02Mトリス−塩酸緩衝液
(PH7.2)1000mlで洗浄した後、2.0の0.15M塩化
ナトリウムを含む0.02Mトリス−塩酸緩衝液(PH
7.2)と2.0の0.3M塩化ナトリウムを含む0.02M
トリス−塩酸緩衝液(PH7.2)とを用いて、グラ
ジエンターによる塩化ナトリウム直線塩濃度勾配
によつて溶出を行なつた。流速90ml/時の条件で
18mlずつ分画して活性画分を採取した。 活性画分を0.1Mの塩化ナトリウムを含む
0.02Mトリス−塩酸緩衝液(PH7.2)に対して透
析した後、同緩衝液であらかじめ平衡化した
DEAE−セフアロースCL−6Bのカラム(2.5×
3.0cm)での再クロマトグラフイーに付した。吸
着された本生理活性物質を350mlのカラム平衡化
緩衝液と350mlの0.3M塩化ナトリウムを含む
0.02Mトリス−塩酸緩衝液(PH7.2)とを用いて、
グラジエンターによる塩化ナトリウム直線塩濃度
勾配によつて溶出を行なつた。流速25ml/時の条
件で7mlずつ分画して活性画分を採取し、濃縮し
た。 次いで、該濃縮液を1.0M塩化ナトリウムを含
む0.01Mトリス−塩酸緩衝液(PH7.8)で平衡化
したセフアクリルS−200のカラムに付し、同緩
衝液で溶出した。ゲル過によつて得られた活性
画分濃縮液を0.02Mリン酸緩衝液(PH7.1)に対
して一夜透析した後、あらかじめ同緩衝液で平衡
化したブルーセフアロースCL−6B(フアルマシ
ア社製)のカラム(1.0××10cm)に付した。流
速2.5ml/時、3ml/分画の条件下に同緩衝液で
充分洗浄した後、1.5M塩化ナトリウムを含む
0.02Mリン酸緩衝液(PH7.1)50mlで吸着物質を
溶離した。吸着画分には活性が認められず、すべ
ての活性は非吸着画分に回収された。これを集め
て凍結乾燥して、原血清に比べて30000倍の純度
を有する本生理活性物質の精製物を得た。全段階
を通しての活性回収率は77%であつた。 実施例 3 6週令のddY雌マウスにホルマリンにて死菌処
理したPropionibacterium acnes(Corynebacte
−rium parvum;ウエルカム社、英国)1mgを
腹腔内投与し、10日後エンドトキシン(大腸菌
026:B6由来のリポポリサツカライド)10μgを
静脈内注射し、2時間後に眼窩静脈叢より毛細管
ピペツトを用いて採血した。採取した血液は、
3000rpm、15分間遠心分離して血球成分を除去し
た。このようにして、10240〜51200単位/mlの力
価を有するマウス血清が得られた。 該血清500mlを0.2M塩化ナトリウムを含む
0.05Mトリス−塩酸緩衝液(PH7.8)に対して一
夜透析した。該透析血清をブフナーロート上で、
あらかじめ同緩衝液で平衡化したDEAE−セフア
デツクスA−50(乾燥重量で500g)に徐々に付
し、本生理活性物質を吸着させた。次いで、イオ
ン交換体容積の3倍量の同緩衝液でイオン交換体
を洗浄して非吸着物質を除去した。次いで、洗浄
時に用いたと同容量の1.0M塩化ナトリウムを含
む0.02Mトリス−塩酸緩衝液(PH7.8)で本生理
活性物質を溶出させた。この段階での活性回収率
は100%、精製度は原血清の36倍であつた。 該溶出液を限外過により濃縮した後、ゲル
過を行なつた。セフアデツクスG−200のカラム
(3.5×95cm)は、0.7M塩化ナトリウムを含む
0.02Mトリス−塩酸緩衝液(PH7.8)で平衡化し
ておき、同緩衝液を用い流速40ml/時で溶出を行
なつた。本生理活性物質は、アルブミン画分の後
半部より単一なピークとして画分された。活性画
分限外過により濃縮した。この段階では活性回
収率80%、精製度6.5倍であり、全段階を通して
は活性回収率80%、精製度240倍であつた。 該濃縮液は、0.02Mリン酸緩衝液(PH7.1)に
対して透析した後、同緩衝液で平衡化したアフイ
ーゲルブルー(バイオーラツド社製)のカラム
(1.0×10cm)に付し、同緩衝液にて溶出した。流
速はすべて2.5ml/時で行なつた。活性は非吸着
画分に溶出されてきた。この画分を集め、凍結乾
燥して本生理活性物質の精製物を得た。この段階
では、活性回収率81%、精製度5倍であり、全段
階を通しては活性回収率65%、精製度1200倍であ
つた。なお、本生理活性物質の精製物の比活性は
約2.4×105単位/mgであつた。 実施例 4 本生理活性物質を含有するマウス血清600mlを
0.02Mトリス−塩酸緩衝液(PH7.8)300mlで希釈
した後、0.1Mの塩化ナトリウムを含む0.02Mト
リス−塩酸緩衝液(PH7.8)であらかじめ平衡化
したDEAE−セフアロースCL−6Bのカラム(6
×36cm)に、除々に付した。次いで、カラム平衡
化緩衝液500mlで洗浄した後、1.5の0.3M塩化
ナトリウムを含む0.02Mトリス−塩酸緩衝液(PH
7.8)とを用いて、グラジエンターによる塩化ナ
トリウム直線塩濃度勾配によつて溶出を行なつ
た。流速75ml/時の条件で18mlずつ分画して活性
画分を採取し、濃縮した。 次いで、該濃縮液を1.0M塩化ナトリウムを含
む0.01Mリン酸緩衝液(PH7.2)であらかじめ平
衡化したセフアクリルS−200のカラム(5×80
cm)に付し、同緩衝液で溶出した。流速63ml/時
の条件で10mlずつ画分して活性画分を採取し、濃
縮した。該濃縮液を実施例3と同様の条件下でア
フイーゲルブルーのカラムを用いるアフイニテイ
ークロマトグラフイーに付して、原血清に比べて
1100倍の純度を有する本生理活性物質の精製物を
得た。全段階を通しての活性回収率は49%であつ
た。
[Table] On the other hand, for normal cells such as human and mouse cultured fibroblasts, the purified product of this physiologically active substance
Even at 2×10 6 units, no cell killing effect was shown. Furthermore, BALB/
In a test in which the purified product of this physiologically active substance was administered to C mice and A/Jax mice bearing tumors with neuroblastoma Neuro-2a, there was a significant difference compared to the control group (physiological saline administration group). Suppression and regression of cancer growth were observed. In addition, in some individuals, established cancers regressed and disappeared without causing hemorrhagic necrosis. The purified product of this physiologically active substance has an extremely excellent anticancer effect and has little species specificity, so it can be expected to be an extremely useful antitumor agent. The present invention will be described in more detail with reference to Examples below, but the present invention is not limited to these Examples. Example 1 A female rabbit (weight 2.5-3 kg) was treated with formalin-killed Propionibacterium acnes (Coryne
−bacterium parvum; Wellcome, UK) 50
mg was injected via the ear vein. Eight days later, 100 μg of endotoxin (lipopolysaccharide derived from water coli 026:B6, manufactured by Difco, USA) was injected into the rabbit via the ear vein, and 2 hours later, whole blood was collected from the heart. The collected blood was centrifuged at 5000 rpm for 30 minutes to remove blood cells and insoluble solids. 1200 ml of serum with a titer of 12800 units/ml was obtained from 20 rabbits. After diluting the serum with 600 ml of 0.02M Tris-HCl buffer (PH7.8), DEAE-Sepharose CL- which had been equilibrated in advance with 0.02M Tris-HCl buffer (PH7.8) containing 0.1M sodium chloride was added. 6B
(manufactured by Pharmacia) column (6 x 36 cm),
It was added gradually. Then add 1000ml of column equilibration buffer (0.02M Tris containing 0.1M sodium chloride).
After washing with hydrochloric acid buffer, PH7.8), 0.1M of 1.5
0.02M Tris-HCl buffer (PH7.8) containing sodium chloride and 1.5% containing 0.3M sodium chloride
Using 0.02M Tris-HCl buffer (PH7.8),
Elution was performed by a linear sodium chloride salt gradient with a gradienter. The active fraction was collected by fractionating into 18 ml portions at a flow rate of 60 ml/hour and concentrated. The activity recovery rate at this stage was 92%, and the degree of purification was 150 times that of the original serum. Next, the concentrated solution was dialyzed into a 0.005M phosphate buffer (PH7.4) containing 0.15M sodium chloride, and then
Gel filtration was performed. Using a Sephacryl S-200 (manufactured by Pharmacia) column (5 x 80 cm), the column was sufficiently equilibrated with the same buffer solution, and then the concentrated solution was applied thereto, and gel permeation elution was performed with the same buffer solution. Flow rate 60ml/
The active fraction was collected by fractionating 10 ml at a time. The active fraction obtained immediately after the albumin fraction was concentrated by ultrafiltration to obtain a purified product of the physiologically active substance. At this stage, the activity recovery rate was 92% and the degree of purification was 52 times, and throughout all stages the activity recovery rate was 85% and the degree of purification was 7800 times. The specific activity of the purified product of this physiologically active substance was approximately 1.4 x 10 6 units/mg protein. Figures 1 and 2 show the patterns of chromatography on a DEAE-Sepharose CL-6B column (first step) and gel filtration on a Sephacryl S-200 column (second step), respectively. Example 2 2200 ml of rabbit serum containing this physiologically active substance was
After diluting with 1200 ml of 0.02 Tris-HCl buffer (PH7.2), add a DEAE-Sepharose CL-6B column ( 8
x 26 cm). It was then washed with 1000 ml of 0.02 M Tris-HCl buffer (PH 7.2) containing 0.13 M sodium chloride, and then washed with 1000 ml of 0.02 M Tris-HCl buffer (PH 7.2) containing 0.13 M sodium chloride.
7.2) and 0.02M containing 0.3M sodium chloride in 2.0
Elution was performed using a tris-hydrochloric acid buffer (PH 7.2) with a sodium chloride linear salt concentration gradient using a gradienter. At a flow rate of 90ml/hour
The active fraction was collected by fractionating 18 ml each. Active fraction containing 0.1M sodium chloride
After dialyzing against 0.02M Tris-HCl buffer (PH7.2), it was equilibrated in advance with the same buffer.
DEAE-Sepharose CL-6B column (2.5×
3.0 cm). The adsorbed biologically active substance was transferred to a column containing 350 ml of column equilibration buffer and 350 ml of 0.3M sodium chloride.
Using 0.02M Tris-HCl buffer (PH7.2),
Elution was performed by a linear sodium chloride salt gradient with a gradienter. The active fraction was collected by fractionating into 7 ml portions at a flow rate of 25 ml/hour and concentrated. Next, the concentrated solution was applied to a Sephacryl S-200 column equilibrated with 0.01M Tris-HCl buffer (PH7.8) containing 1.0M sodium chloride, and eluted with the same buffer. The active fraction concentrate obtained by gel filtration was dialyzed overnight against 0.02M phosphate buffer (PH7.1), and then Bluecepharose CL-6B (Pharmacia) equilibrated with the same buffer was used. The sample was applied to a column (1.0×10 cm) of a commercial manufacturer (Japan). After thorough washing with the same buffer at a flow rate of 2.5 ml/hour and 3 ml/fraction, the solution containing 1.5 M sodium chloride was used.
The adsorbed substances were eluted with 50 ml of 0.02M phosphate buffer (PH7.1). No activity was observed in the adsorbed fraction, and all activity was recovered in the non-adsorbed fraction. This was collected and lyophilized to obtain a purified product of this physiologically active substance that was 30,000 times more pure than the original serum. Activity recovery throughout all stages was 77%. Example 3 Propionibacterium acnes (Corynebacterium acnes) killed with formalin was administered to 6-week-old ddY female mice.
-rium parvum; Wellcome Ltd., UK) 1 mg was administered intraperitoneally, and 10 days later, endotoxin (E. coli
026: B6-derived lipopolysaccharide) 10 μg was intravenously injected, and 2 hours later, blood was collected from the orbital venous plexus using a capillary pipette. The collected blood is
Blood cell components were removed by centrifugation at 3000 rpm for 15 minutes. In this way, mouse serum with a titer of 10240-51200 units/ml was obtained. 500ml of the serum containing 0.2M sodium chloride
Dialysis was performed overnight against 0.05M Tris-HCl buffer (PH7.8). The dialyzed serum was placed on a Buchner funnel,
This physiologically active substance was adsorbed by gradually applying DEAE-Sephadex A-50 (500 g dry weight) equilibrated with the same buffer solution in advance. The ion exchanger was then washed with the same buffer in an amount three times the volume of the ion exchanger to remove non-adsorbed substances. Next, the physiologically active substance was eluted with 0.02M Tris-HCl buffer (PH7.8) containing 1.0M sodium chloride in the same volume as used for washing. At this stage, the activity recovery rate was 100%, and the degree of purification was 36 times that of the original serum. The eluate was concentrated by ultrafiltration and then subjected to gel filtration. Sephadex G-200 column (3.5 x 95 cm) contains 0.7M sodium chloride.
Equilibration was performed with 0.02M Tris-HCl buffer (PH7.8), and elution was performed using the same buffer at a flow rate of 40 ml/hour. This physiologically active substance was fractionated as a single peak from the latter half of the albumin fraction. The active fraction was concentrated by ultrafiltration. At this stage, the activity recovery rate was 80% and the degree of purification was 6.5 times, and throughout all stages the activity recovery rate was 80% and the degree of purification was 240 times. The concentrated solution was dialyzed against 0.02M phosphate buffer (PH7.1) and then applied to a column (1.0 x 10 cm) of Afuigel Blue (manufactured by Biorad) equilibrated with the same buffer. It was eluted with a buffer solution. All flow rates were 2.5 ml/hr. Activity has been eluted in the non-adsorbed fraction. The fractions were collected and lyophilized to obtain a purified product of the physiologically active substance. At this stage, the activity recovery rate was 81% and the degree of purification was 5 times higher, and throughout all stages the activity recovery rate was 65% and the degree of purification was 1200 times higher. The specific activity of the purified product of this physiologically active substance was approximately 2.4×10 5 units/mg. Example 4 600 ml of mouse serum containing this physiologically active substance was
DEAE-Sepharose CL-6B column diluted with 300 ml of 0.02M Tris-HCl buffer (PH7.8) and pre-equilibrated with 0.02M Tris-HCl buffer (PH7.8) containing 0.1M sodium chloride. (6
×36cm). Then, after washing with 500 ml of column equilibration buffer, 0.02 M Tris-HCl buffer containing 0.3 M sodium chloride (PH
7.8), elution was performed using a linear sodium chloride concentration gradient using a gradienter. The active fraction was collected by fractionating into 18 ml portions at a flow rate of 75 ml/hour and concentrated. Next, the concentrated solution was transferred to a Sephacryl S-200 column (5 x 80
cm) and eluted with the same buffer. The active fraction was collected in 10 ml fractions at a flow rate of 63 ml/hour and concentrated. The concentrated solution was subjected to affinity chromatography using an Affigel blue column under the same conditions as in Example 3, and compared to the original serum,
A purified product of this physiologically active substance with a purity of 1100 times was obtained. Activity recovery throughout all stages was 49%.

【図面の簡単な説明】[Brief explanation of drawings]

第1図及び第2図はそれぞれ、実施例1に於け
るDEAE−セフアロースCL−6Bでのクロマトグ
ラフイー及びセフアクリルS−200でのゲル過
のパターンを示す。
FIGS. 1 and 2 respectively show the chromatography pattern using DEAE-Sepharose CL-6B and the gel filtration pattern using Sephacryl S-200 in Example 1.

Claims (1)

【特許請求の範囲】 1 網内系賦活化作用を有する物質の1種又は2
種以上を哺乳動物に投与し、次いでグラム陰性菌
由来のエンドトキシンを注射することによつて、
又は哺乳動物由来の活性化マクロフアージを含む
組識培養系にグラム陰性菌由来のエンドトキシン
を加えることによつて誘発される制ガン作用を有
する蛋白性生理活性物質の粗製溶液を(1)PH6.0〜
9.0、塩濃度0.2M以下の緩衝液を用いて塩基性陰
イオン交換体と接触させて該生理活性物質を吸着
させ、(2)吸着時の塩濃度よりも高塩濃度の緩衝液
を用いて該吸着生理活性物質を該塩基性陰イオン
交換体から溶出させ、次いで(3)該生理活性物質を
含む溶出液を分子量30000〜70000の物質の分離に
適した担体及び溶出液としてPH6.0〜9.0の緩衝液
を用いるゲル濾過に付し、さらに必要に応じて(4)
該生理活性物質画分を下記の構造式 を有する固定化染料を用いるアフイニテイークロ
マトグラフイーに付すことを特徴とする制ガン作
用を有する蛋白性物質の精製方法。 2 該哺乳動物がマウスである特許請求の範囲第
1項記載の精製方法。 3 該哺乳動物がウサギである特許請求の範囲第
1項記載の精製方法。
[Scope of Claims] 1. One or two substances having a reticuloendothelial system activating effect
By administering a species or more to a mammal and then injecting an endotoxin derived from a gram-negative bacterium,
Alternatively, a crude solution of a proteinaceous physiologically active substance with anticancer activity induced by adding endotoxin derived from Gram-negative bacteria to a tissue culture system containing activated macrophages derived from mammals (1) PH6.0 ~
9.0, adsorb the physiologically active substance by contacting it with a basic anion exchanger using a buffer solution with a salt concentration of 0.2M or less, and (2) using a buffer solution with a salt concentration higher than the salt concentration during adsorption. The adsorbed physiologically active substance is eluted from the basic anion exchanger, and then (3) the eluate containing the physiologically active substance is used as a carrier and eluate suitable for separating substances with a molecular weight of 30,000 to 70,000 at a pH of 6.0 to 70,000. Gel filtration using 9.0 buffer, and if necessary (4)
The physiologically active substance fraction has the following structural formula: 1. A method for purifying a proteinaceous substance having anticancer activity, the method comprising subjecting it to affinity chromatography using an immobilized dye having an anticancer effect. 2. The purification method according to claim 1, wherein the mammal is a mouse. 3. The purification method according to claim 1, wherein the mammal is a rabbit.
JP56209841A 1981-12-28 1981-12-28 Purification of physiologically active substance having carcinostatic action Granted JPS57140726A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56209841A JPS57140726A (en) 1981-12-28 1981-12-28 Purification of physiologically active substance having carcinostatic action

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56209841A JPS57140726A (en) 1981-12-28 1981-12-28 Purification of physiologically active substance having carcinostatic action

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP55143197 Division

Publications (2)

Publication Number Publication Date
JPS57140726A JPS57140726A (en) 1982-08-31
JPS6363559B2 true JPS6363559B2 (en) 1988-12-07

Family

ID=16579502

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56209841A Granted JPS57140726A (en) 1981-12-28 1981-12-28 Purification of physiologically active substance having carcinostatic action

Country Status (1)

Country Link
JP (1) JPS57140726A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1984001288A1 (en) * 1982-10-06 1984-04-12 Takeshi Makitsubo Process for extracting tumor necrosis factor from macrophage
JPH088873B2 (en) * 1983-07-28 1996-01-31 大日本製薬株式会社 Method for producing human cancer necrosis factor

Also Published As

Publication number Publication date
JPS57140726A (en) 1982-08-31

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