JPH1189590A - Recovery and purification of protein having epithelial cell growth factor activity - Google Patents

Recovery and purification of protein having epithelial cell growth factor activity

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Publication number
JPH1189590A
JPH1189590A JP9269206A JP26920697A JPH1189590A JP H1189590 A JPH1189590 A JP H1189590A JP 9269206 A JP9269206 A JP 9269206A JP 26920697 A JP26920697 A JP 26920697A JP H1189590 A JPH1189590 A JP H1189590A
Authority
JP
Japan
Prior art keywords
protein
egf
culture
growth factor
activity
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
JP9269206A
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Japanese (ja)
Other versions
JP3737252B2 (en
Inventor
Yasuaki Murahashi
保昭 村橋
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Higeta Shoyu Co Ltd
Original Assignee
Higeta Shoyu Co Ltd
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Priority to JP26920697A priority Critical patent/JP3737252B2/en
Publication of JPH1189590A publication Critical patent/JPH1189590A/en
Application granted granted Critical
Publication of JP3737252B2 publication Critical patent/JP3737252B2/en
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Expired - Fee Related legal-status Critical Current

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  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Peptides Or Proteins (AREA)

Abstract

PROBLEM TO BE SOLVED: To simply and efficiently recover and purify the subject protein, by culturing Bacillus brevis as a host bacterium, adjusting a culture substance containing a product to proper pH to precipitate an admixture protein and subjecting a clear fraction to salting out. SOLUTION: Bacillus brevis is cultured as a host bacterium. A culture material containing a protein having epithelial cell growth factor activity is adjusted to pH 3.0-4.5, preferably pH 3.5-3.9, an admixture protein contained in the culture substance is specific precipitated and the precipitated protein and the cell are removed to give a clear fraction. Then the obtained clear fraction is mixed with a salt (e.g. sodium chloride) to precipitate a protein having epithelial cell growth factor activity. The precipitated fraction is recovered and the coexisting admixture component is separated and removed to recover and purify the objective protein useful as a therapeutic agent for wound, an antiulcer agent, an auxiliary for anticancer agent, etc., simply and efficiently.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、バチルス・ブレビ
スを宿主菌とする遺伝子組換体を培養することによって
生産された上皮細胞増殖因子(Epidermal Growth Facto
r: 以下EGF)活性を有するタンパク質の回収精製法
に関するものである。更に、詳細には、本発明はEGF
活性を有するタンパク質をコードする遺伝子で形質転換
したバチルス・ブレビスを培養し、その培養物からEG
F活性を有するタンパク質を回収精製する方法に関する
ものであって、特に工業的大量処理に適した簡便且つ効
率的なタンパク質の回収精製方法に関するものである。
[0001] The present invention relates to an epidermal growth factor produced by culturing a recombinant using Bacillus brevis as a host bacterium.
r: hereinafter referred to as a method for recovering and purifying a protein having EGF) activity. More particularly, the present invention relates to EGF
Bacillus brevis transformed with a gene encoding an active protein is cultured, and EG is purified from the culture.
The present invention relates to a method for recovering and purifying a protein having F activity, and more particularly to a simple and efficient method for recovering and purifying a protein suitable for industrial mass processing.

【0002】[0002]

【従来の技術】EGFは、ヒトや馬の尿中やウサギ、ラ
ットおよびマウスの顎下腺から単離されており、哺乳動
物の種々の組織中に存在していることが知られている
(Adv. Metab. Dis., 8, 265(1975))。ヒト上皮細胞増
殖因子(human Epidermal Growth Factor: 以下h−EG
F)は、53個のアミノ酸からなる分子量約6,000
のペプチドで、分子内に3ケ所のジスルフィド結合を持
ち、配列番号1に示されるアミノ酸配列であることが知
られている(H.Gregory, Nature, 257, 325(1975))。
2. Description of the Related Art EGF has been isolated from urine of humans and horses and submandibular glands of rabbits, rats and mice, and is known to be present in various tissues of mammals ( Adv. Metab. Dis., 8 , 265 (1975)). Human epidermal growth factor (h-EG)
F) has a molecular weight of about 6,000 consisting of 53 amino acids.
Is known to have three disulfide bonds in the molecule and to have the amino acid sequence shown in SEQ ID NO: 1 (H. Gregory, Nature, 257 , 325 (1975)).

【0003】EGFの生理作用は、細胞増殖作用、胃酸
分泌抑制作用、抗潰瘍作用、消化管粘膜保護作用、DN
A合成促進作用、角膜修復作用、カルシウム遊離促進作
用、創傷治癒促進作用、抗炎症作用、鎮痛作用、肝細胞
障害抑制作用及び毛胞退縮作用などが報告されている
(日本組織培養学会編、細胞成長因子、20頁、朝倉書
店1984年)。EGFはこのような作用を有すること
から創傷治癒薬、抗潰瘍剤、抗癌剤補助剤など様々の分
野で応用が試みられている(BIO INDUSTRY, 8, 275(199
1))。
The physiological effects of EGF include cell proliferation, gastric acid secretion, anti-ulcer, gastrointestinal mucosa protection, and DN.
It has been reported that A-synthesis promoting action, corneal repair action, calcium release promoting action, wound healing promoting action, anti-inflammatory action, analgesic action, hepatocellular damage inhibitory action, hair follicle retraction action, etc. Growth Factor, page 20, Asakura Shoten 1984). Since EGF has such an effect, its application has been attempted in various fields such as a wound healing agent, an antiulcer agent, and an anticancer agent adjuvant (BIO INDUSTRY, 8 , 275 (199)
1)).

【0004】このようにEGFについて種々の応用研究
が進められている一方、EGFを安定に供給可能とする
生産方法についても種々検討が加えられている。
[0004] As described above, various applications of EGF have been studied, and various studies have been made on production methods capable of stably supplying EGF.

【0005】例えば、バチルス・ブレビスHPD31
Bacillus brevis HPD31: なお、この菌株はバチルス
・ブレビスH102(FERM BP−1087)と同
一菌株である)はタンパク質を菌体外に分泌生産し、培
養液中にタンパク質分解酵素を生産しない菌株であり
(特公平4−74997)、遺伝子組換えの宿主菌とし
て様々なタンパク質の生産に利用されている。恵比須ら
は、このバチルス・ブレビスHPD31を宿主菌として
h−EGFの大量生産技術を確立し、h−EGFを培養
液中に約3g/L分泌生産させることに成功している
(特開平6−133782)。また高木らは、EGF活
性を有する新規なタンパク質を創製し、バチルス・ブレ
ビスHPD31を用いその高生産に成功している(特願
平8−123970)。
For example, Bacillus brevis HPD31
( Bacillus brevis HPD31: This strain is the same strain as Bacillus brevis H102 (FERM BP-1087)) is a strain that secretes and produces proteins outside the cells and does not produce proteolytic enzymes in the culture solution. (JP-B 4-74997), which is used as a host cell for genetic recombination for the production of various proteins. Ebisu et al. Have established a mass production technique of h-EGF using Bacillus brevis HPD31 as a host bacterium, and have succeeded in secreting and producing about 3 g / L of h-EGF in a culture solution (Japanese Unexamined Patent Publication No. 133782). Takagi et al. Have created a novel protein having EGF activity and succeeded in high production thereof using Bacillus brevis HPD31 (Japanese Patent Application No. 8-123970).

【0006】しかし、遺伝子組換え技術を適用し培養液
中に分泌生産されたEGFまたはEGF活性を有するタ
ンパク質を医薬品などに開発するには、培養物中に混在
している菌体、培地由来の成分や同時に分泌生産される
夾雑タンパク質やその他の代謝産物などの夾雑物を除去
し、目的とするEGF活性を有するタンパク質のみを回
収精製する必要がある。この精製工程は簡便でかつ工程
数も少ない方がよく、特に精製を工業規模で行う場合に
は精製工程が複雑であると多大な設備投資が必要であ
り、その為生産コストも高くなってしまうという問題が
生じる。
However, in order to develop EGF or a protein having EGF activity secreted and produced in a culture solution into a drug or the like by applying the gene recombination technique, it is necessary to use a mixture of cells and media derived from the medium mixed in the culture. It is necessary to remove contaminants such as components, contaminant proteins secreted and produced at the same time, and other metabolites, and to recover and purify only the protein having the desired EGF activity. It is better that this purification step is simple and the number of steps is small. Particularly, when the purification is performed on an industrial scale, if the purification step is complicated, a large capital investment is required, and the production cost is also increased. The problem arises.

【0007】[0007]

【発明が解決しようとする課題】本発明は、このような
技術上ないし工業上の必要性に鑑みてなされたものであ
って、バチルス・ブレビスを宿主菌とする異種遺伝子産
物の生産において、菌体を含む培養物中からの効率的な
回収精製技術を提供することにある。即ち、本発明は、
バチルス・ブレビスの培養物中に分泌生産されたEGF
活性を有するタンパク質を共存する成分から分離し、簡
便かつ高収率に回収精製する方法を提供するものであっ
て、特に工業的な見地から、本発明は、EGF活性を有
するタンパク質の回収精製に特に適した簡便且つ効率的
な大量処理システムを新たに開発し、これを提供する目
的でなされたものである。
SUMMARY OF THE INVENTION The present invention has been made in view of the above technical and industrial needs, and is directed to the production of a heterologous gene product using Bacillus brevis as a host bacterium. An object of the present invention is to provide an efficient recovery and purification technique from a culture containing a body. That is, the present invention
EGF secreted into Bacillus brevis culture
The present invention provides a method for separating a protein having an activity from coexisting components and recovering and purifying the protein in a simple and high yield. From an industrial point of view, the present invention relates to a method for recovering and purifying a protein having an EGF activity. It has been made for the purpose of newly developing and providing a particularly suitable simple and efficient mass processing system.

【0008】[0008]

【課題を解決するための手段】本発明者らは、EGF活
性を有するタンパク質をバチルス・ブレビスの培養物中
から効率よく回収精製する方法について鋭意研究を重ね
た結果、培養物のpHを特定の範囲に調整すると、バチ
ルス・ブレビスの培養物中に含まれる夾雑タンパク質の
大部分が特異的に凝集沈殿し、凝集沈殿画分及び菌体を
効率よく除くことが可能であること、更に、清澄画分に
塩を加えることによりEGF活性を有するタンパク質を
特異的に凝集沈殿させ膜濾過または遠心分離することに
より非常に簡便かつ効率よくEGF活性を有するタンパ
ク質を回収精製できるという有用な新知見を得た。本発
明は、この有用新知見に基き更に研究の結果、遂に完成
されたものである。
Means for Solving the Problems The present inventors have conducted intensive studies on a method for efficiently recovering and purifying a protein having EGF activity from a Bacillus brevis culture, and as a result, the pH of the culture was determined to be a specific value. When adjusted to the range, most of the contaminating proteins contained in the culture of Bacillus brevis are specifically aggregated and precipitated, and it is possible to efficiently remove the aggregated precipitate fraction and bacterial cells. A useful new finding has been obtained that a protein having EGF activity can be collected and purified very simply and efficiently by membrane filtration or centrifugation by adding a salt to the protein to specifically aggregate and precipitate the protein having EGF activity. . The present invention has been finally completed as a result of further research based on this useful new finding.

【0009】すなわち本発明は、EGF活性を有するタ
ンパク質を含有するバチルス・ブレビスの培養物をpH
調整によって該培養物中に含まれる大部分の夾雑タンパ
ク質を特異的に沈殿させ、これを除去した後、更に、清
澄画分に塩を加えてEGF活性を有するタンパク質を沈
殿させこれを膜濾過または遠心分離によって、共存する
夾雑物から分離回収することを特徴とするEGF活性を
有するタンパク質の回収精製法に関するものである。
That is, the present invention provides a method for preparing a culture of Bacillus brevis containing a protein having EGF activity.
After adjustment, most of the contaminating proteins contained in the culture were specifically precipitated, and after removal of the proteins, salts were added to the clarified fraction to precipitate proteins having EGF activity. The present invention relates to a method for recovering and purifying a protein having EGF activity, which comprises separating and recovering from coexisting contaminants by centrifugation.

【0010】[0010]

【発明の実施の形態】本発明は、EGF活性を有するタ
ンパク質を含有するバチルス・ブレビスの培養物を、下
記工程(a)〜(b)により共存する夾雑タンパク質や
その他の夾雑物よりEGF活性を有するタンパク質を回
収精製する方法に関するものである。
BEST MODE FOR CARRYING OUT THE INVENTION According to the present invention, a culture of Bacillus brevis containing a protein having EGF activity is prepared by removing EGF activity from contaminating proteins and other contaminants by the following steps (a) and (b). The present invention relates to a method for recovering and purifying a protein having the same.

【0011】すなわち本発明を実施するには、該培養物
について、下記工程(a)〜(b)にしたがって処理す
ればよく、これらの処理により、該タンパク質を効率的
に回収精製することができる。 (a)−1:該培養物のpHを3.0〜4.5(好適に
は3.5〜3.9)に調整して、該培養物に含まれる夾
雑タンパク質を沈殿させ; (a)−2:(a)−1で生じた沈殿及び菌体を分離除
去し、EGF活性を有するタンパク質を含有する清澄画
分を得; (b)−1:(a)−2で得た清澄画分に塩を加えて、
EGF活性を有するタンパク質を沈殿させ; (b)−2:(b)−1で生じた沈殿を回収する。
That is, in order to carry out the present invention, the culture may be treated according to the following steps (a) and (b), and the protein can be recovered and purified efficiently by these treatments. . (A) -1: adjusting the pH of the culture to 3.0 to 4.5 (preferably 3.5 to 3.9) to precipitate contaminating proteins contained in the culture; ) -2: The precipitate formed in (a) -1 and the cells were separated and removed to obtain a clarified fraction containing a protein having EGF activity; (b) -1: The clarified fraction obtained in (a) -2 Add salt to the fraction,
(B) -2: recovering the precipitate generated in (b) -1.

【0012】本発明の回収精製方法は、EGF活性を有
するタンパク質を含有するバチルス・ブレビスの培養物
に対して適用できる。具体的には、バチルス・ブレビス
HPD31はh−EGFやEGF活性を有するタンパク
質を菌体外に高生産するので該菌株の該培養物に本発明
の回収精製法が有効に適用できる。
The method for recovery and purification of the present invention can be applied to a Bacillus brevis culture containing a protein having EGF activity. Specifically, Bacillus brevis HPD31 highly produces h-EGF and a protein having EGF activity outside the cells, and thus the recovery and purification method of the present invention can be effectively applied to the culture of the strain.

【0013】本発明方法で回収精製されるEGF活性を
有するタンパク質を具体的に列挙すると、配列番号1の
ヒトEGF、配列番号2のマウスEGF、配列番号3の
ラットEGFや配列番号4〜7のタンパク質(特願平8
−123970)などが挙げられる。また、これらのE
GF活性を有するタンパク質のアミノ酸配列をコードす
る遺伝子は、EGF生産能を有する細胞から単離した遺
伝子でもよいし、化学的に合成した遺伝子を用いてもよ
い。例えば合成遺伝子を用いる場合は、バチルス・ブレ
ビスにおいて最も容認されたコドンでなる遺伝子が好適
である。
Specific examples of proteins having EGF activity recovered and purified by the method of the present invention are as follows: human EGF of SEQ ID NO: 1, mouse EGF of SEQ ID NO: 2, rat EGF of SEQ ID NO: 3, and rat EGF of SEQ ID NO: 4-7. Protein (Japanese Patent Application No. 8
-123970). In addition, these E
The gene encoding the amino acid sequence of the protein having GF activity may be a gene isolated from a cell capable of producing EGF, or a chemically synthesized gene. For example, when a synthetic gene is used, a gene consisting of the most accepted codon in Bacillus brevis is preferred.

【0014】EGF活性を有するタンパク質遺伝子は、
公知の方法でバチルス・ブレビスに組み込めばよく、例
えばモレキュラー・クローニング・ア・ラボラトリーマ
ニュアル第2版、コールド・スプリング・ハーバー・ラボ
ラトリー(Molecular Cloning2nd ed, A Laboratory Ma
nual, Cold Spring Harbor Laboratory, 1989)に記載
の方法で行えばよい。
A protein gene having EGF activity is
It may be incorporated into Bacillus brevis by a known method. For example, Molecular Cloning A Laboratory Manual, 2nd edition, Cold Spring Harbor Laboratory (Molecular Cloning 2nd ed, A Laboratory Ma
nual, Cold Spring Harbor Laboratory, 1989).

【0015】このようにEGF活性を有するタンパク質
をコードする遺伝子で形質転換したバチルス・ブレビス
を通気攪拌培養することによって、EGF活性を有する
タンパク質を含有するバチルス・ブレビスの培養物を得
ることが出来る。
By culturing Bacillus brevis transformed with a gene encoding a protein having EGF activity in this manner, a culture of Bacillus brevis containing a protein having EGF activity can be obtained.

【0016】こうして得たバチルス・ブレビスの培養物
は菌体を含有したまま工程(a)〜(b)で処理するこ
とを基本とするが、予め培養物を膜処理するか遠心分離
する前処理で菌体を除いた後に工程(a)〜(b)で処
理してもよい。即ち、本発明は、該培養物の(a)pH
を3.0〜4.5に調整して、培養物に含まれる夾雑タ
ンパク質を特異的に沈殿させ、この沈殿タンパク質及び
菌体を除去して清澄画分を得る工程、更に、(b)、
(a)で得た清澄画分に塩を加えて、EGF活性を有す
るタンパク質を沈殿させ、この沈殿したタンパク質画分
を共存していた夾雑成分から分離回収するEGF活性を
有するタンパク質の回収精製法である。以下、本発明の
工程(a)〜(b)についてさらに詳しく説明する。
The culture of Bacillus brevis thus obtained is basically treated in the steps (a) to (b) while containing the cells, but the culture is pretreated by membrane treatment or centrifugation. After removing the cells in step (a), the cells may be treated in steps (a) and (b). That is, the present invention relates to (a) pH of the culture.
Is adjusted to 3.0 to 4.5 to specifically precipitate contaminating proteins contained in the culture, and removing the precipitated proteins and cells to obtain a clear fraction;
A salt is added to the clarified fraction obtained in (a) to precipitate a protein having EGF activity, and a method of recovering and purifying a protein having EGF activity in which the precipitated protein fraction is separated and recovered from contaminating components that coexisted therewith It is. Hereinafter, the steps (a) and (b) of the present invention will be described in more detail.

【0017】先ず、EGF活性を有するタンパク質を含
有するバチルス・ブレビスの培養物をそのまま、また
は、遠心分離や膜濾過によって予じめ菌体を除去した培
養物を、次の工程にしたがって処理する。
First, a culture of Bacillus brevis containing a protein having EGF activity, or a culture from which cells have been removed in advance by centrifugation or membrane filtration are treated according to the following steps.

【0018】(a)−1:該培養物のpHを調整するこ
とによって、夾雑タンパク質を沈殿させる。pHは、培
養物に含まれる夾雑タンパク質が特異的に沈殿し、EG
F活性を有するタンパク質が沈殿しない範囲に調整す
る。夾雑タンパク質の主たるものは、バチルス・ブレビ
スHPD31を宿主菌に用いた場合、この菌株が菌体外
に生産する細胞表層タンパク質が主たるもので(HW
P;J.Bacteriol., 172, 1312-1320(1990))、pHを
3.0〜4.5の範囲、更に好ましくは3.5〜3.9
の範囲に調整することで特異的に沈殿させることができ
る。このpHの調整に用いる酸は、塩酸、硝酸、硫酸な
どの酸を用いることでよい。
(A) -1: Contaminant proteins are precipitated by adjusting the pH of the culture. The pH is such that contaminant proteins contained in the culture specifically precipitate,
Adjust so that the protein having F activity does not precipitate. When Bacillus brevis HPD31 is used as a host bacterium, the main contaminating protein is a cell surface protein produced by the strain outside the cells (HW
P; J. Bacteriol., 172 , 1312-1320 (1990)), and the pH is in the range of 3.0 to 4.5, more preferably 3.5 to 3.9.
By adjusting to within the range, specific precipitation can be achieved. As the acid used for adjusting the pH, an acid such as hydrochloric acid, nitric acid, and sulfuric acid may be used.

【0019】(a)−2:(a)−1工程で沈殿した夾
雑タンパク質を除去する工程で、沈殿は遠心分離や膜濾
過によって系外に除去することができる。膜濾過によっ
て除く場合には、EGF活性を有するタンパク質が濾過
され、沈殿したHWPを含む夾雑タンパク質が濃縮され
るポアサイズを有する濾過膜を使用すればよい。例え
ば、0.45μmのポアサイズの濾過膜を用いて精密濾
過を行えば、沈殿は膜上に濃縮され、除去することがで
きる。このとき更に、pH3.0〜4.5の緩衝液を用
いて沈殿を洗浄すれば、EGF活性を有するタンパク質
をより効率よく濾過液に回収することができる。このと
き用いる緩衝液は、EGF活性を有するタンパク質が活
性を失うことのない緩衝液、例えば酢酸緩衝液やリン酸
緩衝液等を用いればよい。こうして、バチルス・ブレビ
スの培養物から夾雑タンパク質が除去され、精製度の高
まったEGF活性を有するタンパク質溶液を得ることが
できる。
(A) -2: In the step of removing contaminating proteins precipitated in the step (a) -1, the precipitate can be removed from the system by centrifugation or membrane filtration. When removing by membrane filtration, a filtration membrane having a pore size in which proteins having EGF activity are filtered and contaminating proteins including precipitated HWP are concentrated. For example, if microfiltration is performed using a filtration membrane having a pore size of 0.45 μm, the precipitate is concentrated on the membrane and can be removed. At this time, if the precipitate is further washed with a buffer having a pH of 3.0 to 4.5, the protein having EGF activity can be more efficiently collected in the filtrate. The buffer used at this time may be a buffer that does not cause the protein having EGF activity to lose its activity, such as an acetate buffer or a phosphate buffer. In this way, contaminating proteins are removed from the Bacillus brevis culture, and a protein solution having enhanced EGF activity can be obtained.

【0020】(b)−1:(a)−2工程で回収した濾
過液に塩を添加して、EGF活性を有するタンパク質を
特異的に沈殿させる。添加する塩は、EGF活性を有す
るタンパク質の凝集性がよく且つ活性を失うことのない
塩であればよく、例えば硫酸アンモニウム、硫酸ナトリ
ウム、リン酸カリウム、硫酸マグネシウム、クエン酸ナ
トリウム、塩化ナトリウムなどが好適に用いることがで
きる。塩濃度はEGF活性を有するタンパク質が沈殿す
る濃度であればよく、9%以上の濃度であればよい。例
えば塩化ナトリウムを用いた場合には9%以上、より好
ましくは12%以上の濃度でよい。
(B) -1: A protein having EGF activity is specifically precipitated by adding a salt to the filtrate collected in the step (a) -2. The salt to be added may be any salt which has good cohesiveness of the protein having EGF activity and does not lose the activity, and for example, ammonium sulfate, sodium sulfate, potassium phosphate, magnesium sulfate, sodium citrate, sodium chloride and the like are preferable. Can be used. The salt concentration may be a concentration at which a protein having EGF activity is precipitated, and may be a concentration of 9% or more. For example, when sodium chloride is used, the concentration may be 9% or more, more preferably 12% or more.

【0021】(b)−2:(b)−1工程で沈殿したE
GF活性を有するタンパク質を回収するには、(a)−
2と同じく遠心分離や膜濾過によって沈殿を回収するこ
とができる。膜濾過によって回収する場合には、沈殿が
膜上に濃縮されるポアサイズを有する膜を使用すればよ
い。例えば、0.45μmのポアサイズの濾過膜を用い
て精密濾過を行い沈殿を濃縮、回収することができる。
このとき加えた塩濃度と同じ塩濃度の緩衝液で沈殿を洗
浄し夾雑物を洗い流すことが出来る。このようにして回
収したEGF活性を有するタンパク質を緩衝液に溶解さ
せた後、透析や膜濾過によって脱塩する。膜濾過で脱塩
を行う場合には、例えば分画分子量5,000の限外濾
過膜を用いて濾過を行い、濃縮が進んだ段階で適量の純
水を加えて十分に塩を除去すればよい。また膜濾過によ
る脱塩は、目的とするEGF活性を有するタンパク質の
濃縮も同時に行えるので、液量をコンパクトにでき、以
降凍結乾燥を行う場合に効果的である。以上のようにし
て、高純度にまで精製されたEGF活性を有するタンパ
ク質を得ることができる。
(B) -2: E precipitated in step (b) -1
To recover a protein having GF activity, (a)-
As in the case of 2, the precipitate can be collected by centrifugation or membrane filtration. When collecting by membrane filtration, a membrane having a pore size in which the precipitate is concentrated on the membrane may be used. For example, the precipitate can be concentrated and recovered by performing microfiltration using a filtration membrane having a pore size of 0.45 μm.
At this time, the precipitate can be washed with a buffer solution having the same salt concentration as the added salt concentration to wash away impurities. The protein having EGF activity thus recovered is dissolved in a buffer, and then desalted by dialysis or membrane filtration. When desalting is performed by membrane filtration, for example, filtration is performed using an ultrafiltration membrane having a molecular weight cutoff of 5,000, and at the stage when the concentration is advanced, an appropriate amount of pure water is added to sufficiently remove salts. Good. In addition, desalting by membrane filtration can simultaneously concentrate the protein having the desired EGF activity, so that the liquid volume can be made compact, which is effective in the subsequent freeze-drying. As described above, a protein having EGF activity purified to high purity can be obtained.

【0022】本発明の回収精製法により、非常に簡便
に、バチルス・ブレビスの培養物からEGF活性を有す
るタンパク質を85%以上の回収率で、90〜95%以
上の純度にまで精製できる。本発明方法で得たEGF活
性を有するタンパク質を各種用途に適用することもでき
るが、さらに純度を上げる必要がある場合には、更に、
クロマトグラフィーなど公知の方法で処理すればさらに
高純度のEGF活性を有するタンパク質を得ることが出
来る。
According to the recovery and purification method of the present invention, a protein having EGF activity can be very easily purified from a Bacillus brevis culture to a purity of 90 to 95% or more with a recovery of 85% or more. The protein having EGF activity obtained by the method of the present invention can be applied to various uses, but when it is necessary to further increase the purity,
A higher-purity protein having EGF activity can be obtained by a known method such as chromatography.

【0023】以下、本発明を実施例により更に詳しく説
明するが、これは例示的なものであり、本発明はこれに
限定されるものではない。
Hereinafter, the present invention will be described in more detail with reference to examples. However, the examples are illustrative and the present invention is not limited thereto.

【0024】[0024]

【実施例1】バチルス・ブレビスHP926(FERM
BP−5382)が保有するプラスミドpHT926
から調製したh−EGF高分泌生産プラスミドpHT1
10EGF(特開平6−133782)でバチルス・ブ
レビスHPD31(FERMBP−1089)をエレク
トロポレーション法(H.Takagi et al. Agric. Biol. C
hem., 53, 3099-3100(1989))で形質転換し、h−EGF
を分泌生産する形質転換体を得た。ここで得た菌株をペ
プトン4%、酵母エキス0.5%、MgSO4 5mM、
MnSO4 1mM、FeSO4 36μM、グルコース2
%、寒天1.5%、pH7.2の寒天培地にて30℃で
一昼夜培養した。これを前記と同じ組成の液体培地1L
に植菌して30℃で一晩振とう培養を行ったものを前培
養液とした。
Embodiment 1 Bacillus brevis HP926 (FERM)
BP-5382).
HT-EGF high secretion production plasmid pHT1 prepared from
Bacillus brevis HPD31 (FERMBP-1089) was electroporated (H. Takagi et al. Agric. Biol. C.) with 10 EGF (Japanese Patent Laid-Open No. 6-133782).
hem., 53 , 3099-3100 (1989)).
Was obtained. The strain obtained here was used for peptone 4%, yeast extract 0.5%, MgSO 4 5 mM,
MnSO 4 1 mM, FeSO 4 36 μM, glucose 2
%, Agar 1.5%, pH 7.2 at 30 ° C. overnight. This was mixed with 1 L of a liquid medium having the same composition as above.
And subjected to shaking culture at 30 ° C. overnight to obtain a pre-culture solution.

【0025】30Lジャーファーメンターに前培養と同
じ組成の生産培地17L分注した後、120℃で15分
間滅菌し、冷却後、前培養液200mlを接種し、攪拌
数200rpm、通気量1vvm、30℃で3日間培養
を行った。
After 17 L of a production medium having the same composition as that of the preculture was dispensed into a 30 L jar fermenter, sterilized at 120 ° C. for 15 minutes, cooled, inoculated with 200 ml of the preculture, stirred at 200 rpm, aerated at 1 vvm, and cooled. Cultivation was carried out at 3 ° C. for 3 days.

【0026】培養物中のh−EGF量をHPLC(カラ
ム:C18−100A、径4mm×長さ250mm、バ
ッファー:0.1%トリフルオロ酢酸(TFA)/H2
O、0.1% TFA/50%アセトニトリル、リニア
グラジエント、検出:UV276nm)で分析し、市販
h−EGF(フナコシ(株)社製)を標準品として同条
件でHPLCを行った時のピーク面積と比較して生産量
を求めた結果、培養物中に1.0g/Lのh−EGFが
生産されていた。
The amount of h-EGF in the culture was determined by HPLC (column: C18-100A, diameter 4 mm × length 250 mm, buffer: 0.1% trifluoroacetic acid (TFA) / H 2 ).
O, 0.1% TFA / 50% acetonitrile, linear gradient, detection: UV 276 nm), and peak area when HPLC was performed under the same conditions using commercially available h-EGF (manufactured by Funakoshi Co., Ltd.) as a standard product. As a result of obtaining the production amount in comparison with, 1.0 g / L of h-EGF was produced in the culture.

【0027】培養物17Lを0.45μmの濾過膜(ペ
リコンカセットシステム(ミリポア社製))を用いて菌
体を除去し、濾過画分にh−EGFを含む培養上清を回
収した。この培養上清のpHを、6N塩酸を用いて3.
8に調整し、HWPを含む夾雑タンパク質を沈殿させ、
前記と同じ濾過膜を用いて濾過を行ってh−EGFを濾
過画分に回収した。また、膜上の夾雑タンパク質を20
mM酢酸緩衝液(pH3.8)1Lで洗浄し、膜上に残
っていたh−EGFを濾過画分に回収した。
The 17 L of the culture was used to remove bacterial cells using a 0.45 μm filtration membrane (Pellicon cassette system (manufactured by Millipore)), and the culture supernatant containing h-EGF in the filtration fraction was recovered. The pH of the culture supernatant was adjusted to 3. using 6N hydrochloric acid.
8 to precipitate contaminating proteins including HWP,
Filtration was performed using the same filtration membrane as described above, and h-EGF was collected in the filtration fraction. In addition, contaminating proteins on the membrane
After washing with 1 L of an mM acetate buffer (pH 3.8), h-EGF remaining on the membrane was collected in a filtration fraction.

【0028】次に、h−EGFを含む濾過画分にNaC
lを12%濃度になるように加え、h−EGFを沈殿さ
せた。これを0.45μmの濾過膜(ペリコンカセット
システム(ミリポア社製))を用いて濾過し、h−EG
Fを膜上に回収した。回収したh−EGFを12% N
aClを含む20mM酢酸緩衝液(pH3.8)1Lで
洗浄濾過を行い不純物を濾過液中に除去した後、膜上の
h−EGF画分を200mlまで濃縮した。こうして回
収したh−EGFを0.1Mトリス緩衝液(pH8.
0)で溶解した。
Next, NaC was added to the filtered fraction containing h-EGF.
1 was added to a concentration of 12% to precipitate h-EGF. This was filtered using a 0.45 μm filtration membrane (Pellicon cassette system (Millipore)) to obtain h-EG.
F was collected on the membrane. The recovered h-EGF was 12% N
After washing and filtering with 1 L of 20 mM acetate buffer (pH 3.8) containing aCl to remove impurities in the filtrate, the h-EGF fraction on the membrane was concentrated to 200 ml. The thus recovered h-EGF was added to a 0.1 M Tris buffer (pH 8.
0).

【0029】このh−EGF含有液を、分画分子量5,
000の限外濾過膜(ペリコンカセットBiomax5(ミリ
ポア社製))を用い、限外濾過して脱塩を行った。50
0ml程度まで濃縮後、塩類を完全に除くために、純水
10Lを徐々に加えながら濾過した。最終的に回収した
h−EGFの回収率および純度を求めた結果、培養物か
らのh−EGFの回収率は90%でその純度は95%で
あった。
This h-EGF-containing solution was subjected to a molecular weight cutoff of 5,
000 ultrafiltration membrane (Pellicon cassette Biomax5 (manufactured by Millipore)) was used for ultrafiltration to desalinate. 50
After concentration to about 0 ml, the mixture was filtered while 10 L of pure water was gradually added to completely remove salts. The recovery rate and purity of the finally recovered h-EGF were determined, and as a result, the recovery rate of h-EGF from the culture was 90% and the purity was 95%.

【0030】[0030]

【実施例2】配列番号7に示すEGF活性を有するタン
パク質のアミノ酸配列をコードする遺伝子を保有するプ
ラスミドpHT−ABC(特願平8−123970)
で、バチルス・ブレビスHPD31(FERM BP−
1089)をエレクトロポレーション法((H.Takagi e
t al. Agric. Biol. Chem., 53, 3099-3100(1989))によ
って形質転換し、EGF活性を有するタンパク質ABC
を分泌生産する形質転換体を得た。
Example 2 Plasmid pHT-ABC carrying a gene encoding the amino acid sequence of a protein having EGF activity shown in SEQ ID NO: 7 (Japanese Patent Application No. 8-123970)
In, Bacillus Brevis HPD31 (FERM BP-
1089) by electroporation ((H. Takagi e
Agric. Biol. Chem., 53 , 3099-3100 (1989)) and a protein ABC having EGF activity.
Was obtained.

【0031】ここで得た菌株を、ペプトン4%、酵母エ
キス0.5%、MgSO4 5mM、MnSO4 1mM、
FeSO4 36μM、グルコース2%、寒天1.5%、
pH7.2の寒天培地にて30℃で一昼夜培養した。こ
れを前記と同じ組成の液体培地100mlを500ml
三角フラスコに分注し、120℃、15分間滅菌し、冷
却後に接種して30℃で一晩振とう培養を行ったものを
前培養液とした。
The strain obtained here was prepared by adding 4% of peptone, 0.5% of yeast extract, 5 mM of MgSO 4 , 1 mM of MnSO 4 ,
FeSO 4 36 μM, glucose 2%, agar 1.5%,
The cells were cultured overnight at 30 ° C. on a pH 7.2 agar medium. 500 ml of 100 ml of liquid medium of the same composition as above
The mixture was dispensed into an Erlenmeyer flask, sterilized at 120 ° C. for 15 minutes, inoculated after cooling, and cultured with shaking at 30 ° C. overnight to obtain a pre-culture solution.

【0032】2Lジャーファーメンター2本各々に前培
養と同じ組成の生産培地1L分注した後、120℃で1
5分間滅菌し、冷却後、前培養液20mlを接種し、攪
拌数200rpm、通気量1vvm、30℃で3日間培
養を行った。
After dispensing 1 L of a production medium having the same composition as that of the preculture to each of two 2 L jar fermenters,
The mixture was sterilized for 5 minutes, cooled, inoculated with 20 ml of the pre-culture liquid, and cultured at 30 rpm at a stirring speed of 200 rpm at a ventilation rate of 1 vvm for 3 days.

【0033】培養物中のタンパク質ABCの量をHPL
C(カラム:C18−100A、径4mm×長さ250
mm、バッファー:0.1%トリフルオロ酢酸(TF
A)/H2O、0.1% TFA/50%アセトニトリ
ル、リニアグラジエント、検出:UV276nm)で分
析し、市販h−EGF(フナコシ(株)社製)を標準品
として同条件でHPLCを行った時のピーク面積と比較
して生産量を推定した結果、培養物中に約0.8g/L
のタンパク質が生産されていた。
The amount of protein ABC in the culture was determined by HPL
C (column: C18-100A, diameter 4 mm x length 250)
mm, buffer: 0.1% trifluoroacetic acid (TF
A) / H 2 O, 0.1 % TFA / 50% acetonitrile, linear gradient, detection: analyzed by UV276nm), subjected to HPLC under the same conditions a commercial h-EGF and (Funakoshi Co., Ltd.) as a standard As a result of estimating the production amount in comparison with the peak area at the time of
Protein was being produced.

【0034】この培養物のpHを6N塩酸を用いて3.
8に調整し、HWPを含む夾雑タンパク質を沈殿させ、
濾過膜(ミニタンカセットシステム(ミリポア社製))
を用いて濾過を行ってタンパク質ABCを濾過画分に回
収した。また膜上の夾雑タンパク質及び菌体を20mM
酢酸緩衝液(pH3.8)500mlで洗浄し、更に、
膜上に残っていた少量のタンパク質ABCを濾過画分に
回収した。
The pH of this culture was adjusted using 6N hydrochloric acid.
8 to precipitate contaminating proteins including HWP,
Filtration membrane (Mini-tan cassette system (Millipore))
The protein ABC was collected in the filtration fraction by filtration. 20 mM of contaminating proteins and cells on the membrane
Wash with 500 ml of acetate buffer (pH 3.8),
A small amount of the protein ABC remaining on the membrane was recovered in the filtration fraction.

【0035】次に、h−EGFを含む濾過画分に硫酸ア
ンモニウムを15%濃度になるように加え、h−EGF
を沈殿させた。これを0.45μmの濾過膜(ミニタン
カセットシステム(ミリポア社製))を用いて濾過し、
タンパク質ABCを膜上に回収した。回収したタンパク
質ABCを、15%硫酸アンモニウムを含む20mM酢
酸緩衝液(pH3.8)500mlで洗浄し、不純物を
除去した後、膜上のタンパク質ABC画分を200ml
まで濃縮した。こうして回収したタンパク質ABCを
0.1Mトリス緩衝液(pH8.0)で溶解した。
Next, ammonium sulfate was added to the filtered fraction containing h-EGF to a concentration of 15%.
Was precipitated. This was filtered using a 0.45 μm filtration membrane (Minitan Cassette System (manufactured by Millipore)).
The protein ABC was collected on the membrane. The collected protein ABC was washed with 500 ml of a 20 mM acetate buffer (pH 3.8) containing 15% ammonium sulfate to remove impurities, and then 200 ml of the protein ABC fraction on the membrane was removed.
Concentrated. The thus recovered protein ABC was dissolved in a 0.1 M Tris buffer (pH 8.0).

【0036】このタンパク質ABC含有液を、分画分子
量5,000の限外濾過膜(ペリコンカセットBiomax5
(ミリポア社製))を用いて限外濾過して脱塩を行っ
た。500ml程度まで濃縮後、塩類を完全に除くため
に、純水10Lを徐々に加えながら濾過した。最終的に
回収したEGF活性を有するタンパク質ABCの純度お
よび回収率を求めた結果、培養物からのEGF活性を有
するタンパク質ABCの回収率は推測値85%でその純
度は93%であった。
The protein ABC-containing solution was applied to an ultrafiltration membrane having a molecular weight cutoff of 5,000 (Pellicon cassette Biomax5).
(Millipore)) for desalting. After concentration to about 500 ml, the mixture was filtered while 10 L of pure water was gradually added to completely remove salts. The purity and recovery of the finally recovered protein ABC having EGF activity were determined, and as a result, the recovery of protein ABC having EGF activity from the culture was estimated at 85%, with a purity of 93%.

【0037】[0037]

【発明の効果】本発明は、培養物からEGF活性を有す
るタンパク質を非常に簡便且つ効率的に回収精製する方
法を提供するものであって、特に工業的規模で該タンパ
ク質を回収精製するのに有効である。
Industrial Applicability The present invention provides a method for recovering and purifying a protein having EGF activity from a culture very simply and efficiently, and is particularly useful for recovering and purifying the protein on an industrial scale. It is valid.

【0038】[0038]

【配列表】ヒトEGF、マウスEGF、ラットEGFの
アミノ酸配列を、それぞれ、配列番号1、2、3に示
し、4種の関連タンパク質を、それぞれ、配列番号4、
5、6、7に示す。下記表1〜7に、配列番号1〜7で
示される各配列を示す。
Sequence Listing The amino acid sequences of human EGF, mouse EGF, and rat EGF are shown in SEQ ID NOs: 1, 2, and 3, respectively, and the four types of related proteins are shown in SEQ ID NO: 4, respectively.
The results are shown in 5, 6, and 7. Tables 1 to 7 below show the respective sequences shown in SEQ ID NOs: 1 to 7.

【0039】[0039]

【表1】 [Table 1]

【0040】[0040]

【表2】 [Table 2]

【0041】[0041]

【表3】 [Table 3]

【0042】[0042]

【表4】 [Table 4]

【0043】[0043]

【表5】 [Table 5]

【0044】[0044]

【表6】 [Table 6]

【0045】[0045]

【表7】 [Table 7]

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C12P 21/02 C12N 15/00 ZNAA //(C12N 1/21 C12R 1:08) (C12N 15/09 ZNA C12R 1:08) (C12P 21/02 C12R 1:08) ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification symbol FI C12P 21/02 C12N 15/00 ZNAA // (C12N 1/21 C12R 1:08) (C12N 15/09 ZNA C12R 1:08) (C12P 21/02 C12R 1:08)

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 バチルス・ブレビスを宿主菌として培養
し、生産された上皮細胞増殖因子活性を有するタンパク
質を含有する培養物について、 (a)そのpHを調整して、培養物に含まれる夾雑タン
パク質を特異的に沈殿させ、この沈殿タンパク質及び菌
体を除去して清澄画分を得る工程; (b)得られた清澄画分に塩を加えて、上皮細胞増殖因
子活性を有するタンパク質を沈殿させ、この沈殿したタ
ンパク質画分を回収し、共存していた夾雑成分を分離除
去する工程;の各工程からなること、を特徴とする上皮
細胞増殖因子活性を有するタンパク質の回収精製法。
1. A culture containing a protein having epidermal growth factor activity produced by cultivating Bacillus brevis as a host bacterium, comprising: (a) adjusting the pH thereof to obtain a contaminant protein contained in the culture; Specifically, and removing the precipitated protein and cells to obtain a clear fraction; (b) adding a salt to the obtained clear fraction to precipitate a protein having epidermal growth factor activity. Recovering the precipitated protein fraction and separating and removing coexisting contaminant components.
【請求項2】 工程(a)において、pHを3.0〜
4.5、更に好適には3.5〜3.9に調整すること、
を特徴とする請求項1に記載の回収精製法。
2. In the step (a), the pH is adjusted to 3.0 to 3.0.
4.5, more preferably 3.5 to 3.9,
The method for recovery and purification according to claim 1, characterized in that:
【請求項3】 工程(b)において、塩としては、塩化
ナトリウム、硫酸アンモニウム、硫酸ナトリウム、リン
酸カリウム、硫酸マグネシウム、クエン酸ナトリウムか
ら選ばれる少なくともひとつを使用し、添加濃度を9%
以上、更に好適には12%以上とすること、を特徴とす
る請求項1又は2に記載の回収精製法。
3. In the step (b), as a salt, at least one selected from sodium chloride, ammonium sulfate, sodium sulfate, potassium phosphate, magnesium sulfate and sodium citrate is used, and the concentration of the salt is 9%.
The recovery and purification method according to claim 1 or 2, wherein the content is more preferably 12% or more.
【請求項4】 上皮細胞増殖因子活性を有するタンパク
質が、配列番号1に示したヒト上皮細胞増殖因子、配列
番号2に示したマウス上皮細胞増殖因子、配列番号3に
示したラット上皮細胞増殖因子または配列番号4〜7で
示した何れかのタンパク質の少なくともひとつであるこ
と、を特徴とする請求項1〜3のいずれか1項に記載の
回収精製法。
4. The protein having epidermal growth factor activity is human epidermal growth factor shown in SEQ ID NO: 1, mouse epidermal growth factor shown in SEQ ID NO. 2, and rat epidermal growth factor shown in SEQ ID NO. 4. The method according to claim 1, wherein the method is at least one of the proteins represented by SEQ ID NOs: 4 to 7.
JP26920697A 1997-09-17 1997-09-17 Method for recovering and purifying protein having epidermal growth factor activity Expired - Fee Related JP3737252B2 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018164195A1 (en) * 2017-03-07 2018-09-13 Spiber株式会社 Method for producing purified protein

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018164195A1 (en) * 2017-03-07 2018-09-13 Spiber株式会社 Method for producing purified protein

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