JPH05207874A - Serumless culture medium - Google Patents

Serumless culture medium

Info

Publication number
JPH05207874A
JPH05207874A JP4012923A JP1292392A JPH05207874A JP H05207874 A JPH05207874 A JP H05207874A JP 4012923 A JP4012923 A JP 4012923A JP 1292392 A JP1292392 A JP 1292392A JP H05207874 A JPH05207874 A JP H05207874A
Authority
JP
Japan
Prior art keywords
medium
serum
physiologically active
cells
active substance
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.)
Pending
Application number
JP4012923A
Other languages
Japanese (ja)
Inventor
Atsunori Shindou
敦徳 進藤
Maki Suzuki
摩紀 鈴木
Nobumi Kusuhara
信海 楠原
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP4012923A priority Critical patent/JPH05207874A/en
Publication of JPH05207874A publication Critical patent/JPH05207874A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Enzymes And Modification Thereof (AREA)

Abstract

PURPOSE:To provide a production method for physiologically active substances using a serumless medium. CONSTITUTION:The objective serumless culture medium containing lambda- carrageenan. Using this medium, physiologically active substance-producing cells are cultured to produce physiologically active substances such as tissue-type plasminogen activating factor or monoclonal antibody. This serumless medium, which contains no serum or serum albumin, is inexpensive and stable. With this medium, even when adhesive cells fairly hard to culture are used, debonding of e.g. a microcarrier for the cells from an adherend wall can be suppressed, thus obtaining desired physiologically active substances at amounts equal to or more than those in the case with serum medium.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、動物細胞培養により種
々の生理活性物質を生産させる際に用いられる無血清培
地、およびその培地を利用して生理活性物質を生産する
方法に関する。
TECHNICAL FIELD The present invention relates to a serum-free medium used for producing various physiologically active substances by culturing animal cells, and a method for producing physiologically active substances using the medium.

【0002】[0002]

【従来の技術】近年、遺伝子工学技術や細胞融合技術の
急速な進歩に伴い、種々の有用な生理活性物質を、動物
細胞培養により生産させることが可能になった。従来か
ら、動物細胞用の培地には、細胞増殖工程、生理活性物
質生産工程に係わらず、牛胎児血清あるいは子牛血清の
ような哺乳動物の血清を多量に添加した培地が用いられ
てきた。
2. Description of the Related Art In recent years, with the rapid progress of genetic engineering technology and cell fusion technology, it has become possible to produce various useful physiologically active substances by animal cell culture. Conventionally, as a medium for animal cells, a medium to which a large amount of mammalian serum such as fetal bovine serum or calf serum has been added has been used irrespective of the cell proliferation process and the physiologically active substance production process.

【0003】しかしながら、これらの血清は非常に高価
で、かつ価格の変動が大きいうえに、不安定な液体成分
のため冷凍保存する必要があり、大量の入手が困難であ
るため、培地の経済性、大量供給の点で問題がある。ま
た、血清には原因不明のロット間差があるため、培養液
中の生理活性物質の蓄積量に変動を生じ、生理活性物質
の安定生産に障害となる。その上、血清には多種類の異
種タンパク質が含まれるため、培養液からこれらの血清
由来物質を除去することが非常に煩雑かつ困難であり、
目的の生理活性物質の分離精製における障害にもなって
いた。
However, these sera are very expensive, their prices fluctuate greatly, and because they are unstable liquid components, they must be frozen and stored, and it is difficult to obtain a large amount of them. , There is a problem in terms of mass supply. Further, since there are lot-to-lot differences in serum, the amount of accumulated physiologically active substance in the culture solution fluctuates, which hinders stable production of the physiologically active substance. Moreover, since serum contains many kinds of heterologous proteins, it is very complicated and difficult to remove these serum-derived substances from the culture solution.
It has also been an obstacle in the separation and purification of the target physiologically active substance.

【0004】最近、血清の代わりに血清アルブミンを含
む無血清培地が開発された。しかし、この血清アルブミ
ンも大量に添加する必要があること、依然として高価で
あること、血清同様ロット間差があること、目的の生理
活性物質を分離精製する際に血清アルブミンの除去が困
難であることなどの問題があり、ほとんどの問題点が未
だ解決されていない。
Recently, a serum-free medium containing serum albumin instead of serum has been developed. However, it is necessary to add a large amount of this serum albumin, it is still expensive, there is a lot-to-lot difference like serum, and it is difficult to remove serum albumin when separating and purifying the desired physiologically active substance. However, most of the problems have not been solved yet.

【0005】また、現在までに比較的培養の簡単な浮遊
性細胞を中心として、血清アルブミンを含まない無血清
培地が開発され、市販されてきた(大野・村上編、無血
清細胞培養マニュアル、講談社、P31〜39、198
9年)が、培養の難しい付着性細胞には実質的に使用で
きない、保存期間が短かい、非常に高価であるなど、産
業上使用するには問題点が多い。さらに、付着性細胞の
場合には、血清培地などの適当な増殖培地で増殖させた
後、無血清培地に切り換えると細胞が付着壁から剥離
し、長期間培養できないという問題がある。特に、スケ
−ルアップを目的とした、マイクロキャリヤ−などを用
いるジャ−ファ−メンタ−などの撹拌培養の場合は撹拌
せん断力により細胞はさらに剥離しやすい傾向にある。
Further, to date, serum-free medium containing no serum albumin has been developed and marketed centering on floating cells that are relatively easy to culture (Ono and Murakami, ed., Serum-free cell culture manual, Kodansha). , P31-39, 198
However, there are many problems for industrial use, such as being substantially unusable for adherent cells that are difficult to culture, having a short storage period, and being very expensive. Further, in the case of adherent cells, if the cells are grown in an appropriate growth medium such as serum medium and then switched to serum-free medium, the cells detach from the adherent wall, and there is a problem that the cells cannot be cultured for a long time. In particular, in the case of stirring culture such as a jar fermenter using a microcarrier for the purpose of scale-up, the cells tend to be more easily detached by the stirring shearing force.

【0006】以上のような背景から、付着性細胞、浮遊
性細胞に係わらず、生理活性物質の生産工程だけでも血
清や血清アルブミンを含まない培地で培養可能ならば、
血清のロット間差による生理活性物質生産量の変動、分
離精製における不純物除去の問題が解決できる。さら
に、血清や血清アルブミンを代替する物質が安価であ
り、安定であれば、培地の経済性、大量供給の面での問
題点も大幅に改善することが可能になる。また、これら
の安価な物質の添加により、血清培地と同等以上の量の
生理活性物質を生産できれば、生理活性物質の工業的大
量生産が可能となる。
From the above background, if it is possible to cultivate in a medium containing no serum or serum albumin in the production process of a physiologically active substance, regardless of adherent cells or floating cells,
It is possible to solve the problems of fluctuations in the production amount of physiologically active substances due to the difference between lots of serum and the removal of impurities in separation and purification. Furthermore, if the substance that replaces serum or serum albumin is inexpensive and stable, it becomes possible to greatly improve the problems in terms of economics of the medium and large-scale supply. Further, if the addition of these inexpensive substances can produce a physiologically active substance in an amount equal to or more than that in the serum medium, industrial mass production of the physiologically active substance becomes possible.

【0007】[0007]

【発明が解決しようとする課題】本発明の目的は、血清
や血清アルブミンを含まない生理活性物質生産用培地を
提供することである。本発明の他の目的は、安価で安定
な無血清培地を提供することにある。本発明のさらに他
の目的は、付着性細胞を用いた場合でも細胞の付着壁か
らの剥離を抑える無血清培地を提供することである。本
発明のさらに他の目的は、長期間に渡って無血清培地と
同等以上の量の生理活性物質を生産可能とする無血清培
地を提供することである。本発明のさらに他の目的は、
無血清培地を用いて生理活性物質を生産する方法を提供
することである。
An object of the present invention is to provide a medium for producing a physiologically active substance which does not contain serum or serum albumin. Another object of the present invention is to provide an inexpensive and stable serum-free medium. Still another object of the present invention is to provide a serum-free medium that suppresses detachment of cells from the adhesion wall even when adherent cells are used. Still another object of the present invention is to provide a serum-free medium capable of producing a physiologically active substance in an amount equal to or higher than that of the serum-free medium for a long period of time. Still another object of the present invention is to
It is intended to provide a method for producing a physiologically active substance using a serum-free medium.

【0008】[0008]

【課題を解決するための手段】本発明者らは、上述の問
題点を解決するために鋭意検討した結果、生理活性物質
の生産工程において、通常の動物細胞に用いられている
血清を含まない基本培地にλ−カラギ−ナンを添加する
ことにより、付着性細胞を用いた場合にも、長期間に渡
って血清培地と同等以上の量の生理活性物質を生産でき
ることを見出し、本発明を完成させるに至った。
Means for Solving the Problems As a result of intensive studies for solving the above-mentioned problems, the present inventors have found that the process of producing a physiologically active substance does not include serum that is normally used in animal cells. By adding λ-carrageenan to the basal medium, it was found that, even when adherent cells are used, it is possible to produce a physiologically active substance in an amount equal to or greater than that of the serum medium over a long period of time, and the present invention was completed. Came to let me.

【0009】すなわち、本発明はλ−カラギ−ナンを含
有してなることを特徴とする無血清培地、および生理活
性物質生産細胞を上記無血清培地で培養して生理活性物
質を生産する方法である。
That is, the present invention provides a serum-free medium characterized by containing λ-carrageenan, and a method for culturing physiologically active substance-producing cells in the serum-free medium to produce a physiologically active substance. is there.

【0010】本発明の無血清培地に使用される基本培地
としては、従来から知られている動物細胞培養用の血清
を含まない基本培地のいずれも用いることができる。例
えば、イ−グル最小必須培地、ダルベッコ変法イ−グル
培地、RPMI−1640培地、ハムF−12培地など
が挙げられる。これらの基本培地は複数種を適当な割合
で混合したり、インシュリンやトランスフェリンなどを
添加して使用することも可能である。
As the basal medium used in the serum-free medium of the present invention, any conventionally known serum-free basal medium for culturing animal cells can be used. Examples include Eagle's minimum essential medium, Dulbecco's modified Eagle medium, RPMI-1640 medium, Ham's F-12 medium and the like. It is also possible to mix a plurality of these basic media at an appropriate ratio or to add insulin, transferrin or the like for use.

【0011】本発明の無血清培地に使用されるカラギ−
ナンは、紅藻に含まれる寒天の一種であり、アガロビオ
−スを繰り返し単位とし、硫酸基などが結合した酸性多
糖の一種である。カラギ−ナンは種々の型が知られる
が、本発明の培地にはゲル化能のほとんど無いλ型が使
用される。λ−カラギ−ナンは、一般に市販されてお
り、和光純薬工業やシグマ社などから簡単に入手可能で
ある。
Carrage used in the serum-free medium of the present invention
Nan is a kind of agar contained in red algae, and is a kind of acidic polysaccharide having agarobiose as a repeating unit and having a sulfate group bonded thereto. Although various types of carrageenan are known, λ type, which has almost no gelling ability, is used in the medium of the present invention. [lambda] -carrageenan is generally commercially available and can be easily obtained from Wako Pure Chemical Industries, Sigma Co., and the like.

【0012】本発明におけるλ−カラギ−ナンの培地へ
の添加量はあまり添加し過ぎると付着性細胞の場合には
細胞が付着壁から剥離する傾向が見られるが、10〜1
00mg/lの範囲で使用すれば好ましい結果が得られ
る。
In the present invention, when the amount of λ-carrageenan added to the medium is too much, in the case of adherent cells, the cells tend to be detached from the adherent wall.
When used in the range of 00 mg / l, favorable results are obtained.

【0013】また、その他の成分として、糖、アミノ
酸、核酸関連物質、ビタミン、微量元素、プロテア−ゼ
阻害剤などを必要に応じて基本培地に添加しても差し支
えない。そのような成分としては、次のような例が挙げ
られる。例えば、一般に糖源としてグルコ−スが用いら
れるが、培養中に培地に蓄積する乳酸の量を減らす目的
で、ガラクト−スなどを添加する場合が挙げられる。ま
た、例えば、プロリン要求性細胞(チャイニ−ズハムス
タ−卵巣細胞など)を、ダルベッコ変法イ−グル培地
(この培地はプロリンを含まない)を基本培地とする本
発明の無血清培地で培養する際に、L−プロリンを適量
添加する。また、例えば、メタロチオネインのプロモ−
タ−を接続したプラスミドで形質転換した組み換え細胞
により、生理活性物質を生産させる場合には、亜鉛、カ
ドミウムもしくはその塩を本発明の無血清培地に添加す
る。また、例えば、本発明の無血清培地において、組織
型プラスミノ−ゲン活性化因子の一本鎖の方を二本鎖の
ものよりも多く生産させたい場合には、アプロチニン、
ε−アミノカプロン酸、p−アミノメチル安息香酸など
のプロテア−ゼ阻害剤を添加する。また、例えば、生理
活性物質の生産量を増大させる目的で本発明の無血清培
地に酪酸または、プロピオン酸もしくはそれらの塩を添
加する場合などが挙げられる。
As other components, sugar, amino acids, nucleic acid-related substances, vitamins, trace elements, protease inhibitors and the like may be added to the basal medium as needed. Examples of such components include the following. For example, glucose is generally used as a sugar source, and examples thereof include the case of adding galactose or the like for the purpose of reducing the amount of lactic acid accumulated in the medium during culture. In addition, for example, when culturing proline-requiring cells (such as Chinese Hamster-ovary cells) in the serum-free medium of the present invention using Dulbecco's modified Eagle medium (this medium does not contain proline) as a basic medium Then, an appropriate amount of L-proline is added. In addition, for example, a metallothionein promoter
When a physiologically active substance is produced by a recombinant cell transformed with the plasmid to which the target is connected, zinc, cadmium or a salt thereof is added to the serum-free medium of the present invention. Further, for example, in the serum-free medium of the present invention, if it is desired to produce more single chain of tissue-type plasmin-ogen activator than double chain, aprotinin,
A protease inhibitor such as ε-aminocaproic acid or p-aminomethylbenzoic acid is added. Further, for example, the case of adding butyric acid, propionic acid or a salt thereof to the serum-free medium of the present invention for the purpose of increasing the production amount of the physiologically active substance can be mentioned.

【0014】また、本発明の無血清培地は、血清や血清
アルブミンを添加しても使用可能であることは言うまで
もない。しかし、本発明の目的の1つは、生理活性物質
の生産工程において、培地から血清や血清アルブミンを
除去することにあるので、生理活性物質を培養液から回
収する際、血清や血清アルブミンにより支障を来す場合
は、血清や血清アルブミンの使用は好ましくない。
Needless to say, the serum-free medium of the present invention can be used even if serum or serum albumin is added. However, one of the objects of the present invention is to remove serum and serum albumin from the medium in the process of producing the physiologically active substance, so that when the physiologically active substance is recovered from the culture medium, it is disturbed by serum and serum albumin. If it occurs, the use of serum or serum albumin is not preferable.

【0015】本発明の無血清培地は、種々の生理活性物
質の生産に使用される。そのような生理活性物質とし
て、例えば各種酵素類(組織型プラスミノ−ゲン活性化
因子など)、各種モノクロ−ナル抗体(ヒトモノクロ−
ナル抗体、マウスモノクロ−ナル抗体など)、各種リン
ホカイン(インタ−フェロンなど)、各種ホルモン(ヒ
ト成長ホルモンなど)などを挙げることが出来、本発明
の無血清培地を用いて生産することが出来る。
The serum-free medium of the present invention is used for producing various physiologically active substances. Examples of such physiologically active substances include various enzymes (tissue-type plasminogen activator, etc.), various monoclonal antibodies (human monoclonal antibodies).
Null antibodies, mouse monoclonal antibodies, etc.), various lymphokines (interferon, etc.), various hormones (human growth hormone, etc.), and the like, which can be produced using the serum-free medium of the present invention.

【0016】そのような生理活性物質の生産に使用され
る細胞としては、比較的培養の難しい付着性細胞はもち
ろんのこと、浮遊性細胞のいずれにも用いることがで
き、動物由来の各種細胞の培養による生理活性物質の生
産が可能である。例えば、繊維芽細胞、上皮性細胞、リ
ンパ球系細胞、これらの形質転換細胞、ハイブリド−マ
などが挙げられる。
As cells used for the production of such physiologically active substances, not only adherent cells which are relatively difficult to culture but also floating cells can be used. It is possible to produce physiologically active substances by culturing. Examples include fibroblasts, epithelial cells, lymphoid cells, transformed cells thereof, hybridomas and the like.

【0017】生理活性物質を生産するための生理活性物
質生産細胞の培養方法は、特に限定されるものではな
く、通常の動物細胞培養の方法で行うことが出来る。例
えば、マルチウエルプレ−ト、ペトリ皿、組織培養フラ
スコ、ロ−ラ−ボトル、スピナ−フラスコ、ジャ−ファ
−メンタ−や、マイクロキャリヤ−、ホロ−ファイバ−
などを用い、使用する細胞に適した増殖用の培地(血清
アルブミンや増殖因子を含む無血清培地、あるいは血清
を添加した培地)に細胞の適当量を植え込み、適温、適
切な時間増殖させた後、増殖用の培地を除去し、本発明
の培地に切り換えて、生理活性物質を生産させる。
The method for culturing the physiologically active substance-producing cells for producing the physiologically active substance is not particularly limited, and a usual animal cell culture method can be used. For example, multi-well plates, petri dishes, tissue culture flasks, roller bottles, spinner flasks, jar fermenters, microcarriers, hollow fibers.
After inoculating an appropriate amount of cells into a growth medium (serum-free medium containing serum albumin or growth factors, or medium containing serum) suitable for the cells to be used, grow at a suitable temperature for a suitable time. , The medium for growth is removed, and the medium of the present invention is replaced to produce a physiologically active substance.

【0018】また、例えば、上記同様の方法により生理
活性物質を生産させた後、数日間毎に培養液を回収する
と共に、新鮮な本発明の培地を加えると言う操作を繰り
返し生産を継続する。また、例えば、使用する細胞に適
した増殖用の培地に細胞の適当量を植え込み、適温、適
切な時間増殖させた後、本発明の培地を連続的に添加す
ると同時に増殖用の培地を抜き出すパ−ヒュ−ジョン培
養を行い、血清アルブミンや増殖因子、血清を徐々に除
去し、最終的には完全に除去し、生理活性物質を生産さ
せる。
Further, for example, after the physiologically active substance is produced by the same method as described above, the culture solution is collected every several days and the operation of adding the fresh medium of the present invention is repeated to continue production. In addition, for example, after injecting an appropriate amount of cells into a growth medium suitable for the cells to be used and growing the cells at an appropriate temperature for an appropriate time, the medium of the present invention is continuously added, and at the same time, the growth medium is extracted. -Huth culture is performed to gradually remove serum albumin, growth factors, and serum, and finally completely remove them to produce a physiologically active substance.

【0019】[0019]

【実施例】以下、実施例により本発明を詳細に説明す
る。 実施例1.付着性細胞であり、組織型プラスミノ−ゲン
活性化因子(以後tPAと略す)を生産する、組み換え
マウスC−127細胞、hT−382株(特開昭62−
126978)を使用した。ベルコ社の500mlスピ
ンナ−フラスコにマイクロキャリヤ−(Cytodex
1、ファルマシア社)を2gと、予め不活性化させた牛
胎児血清(以後FCSと略す)を10%含むダルベッコ
変法イ−グル培地(増殖用の培地)を500ml 仕込
んだ。上記の種細胞を7×107 個播種し、37℃、4
0rpmの条件で培養を開始した。増殖3日目に、撹拌
を停止し、細胞の付着したマイクロキャリヤ−を沈降さ
せ、培養液を吸引除去した。新鮮な増殖用の培地を加
え、再び培養を続けた。増殖4日目に上記同様の操作に
より生産培地に切り換え、tPAを生産させた。生産用
の培地には、塩化亜鉛20μM、ε−アミノカプロン酸
10mMを含むダルベッコ変法イ−グル培地に、表1
(表1)に示した種々の物質を添加した培地を用いた。
2日間培養した後、培養液中のtPAをELISA法に
より定量した。また、顕微鏡によりマイクロキャリヤ−
からの細胞の剥離の程度を観察した。以上の結果を表1
(表1)に示した。
The present invention will be described in detail below with reference to examples. Example 1. Recombinant mouse C-127 cells, hT-382 strain, which are adherent cells and produce tissue-type plasmin-gen activator (hereinafter abbreviated as tPA) (Japanese Patent Laid-Open No. 62-
126978) was used. Microcarriers (Cytodex) in a Belco 500 ml spinner flask.
(1. Pharmacia) and 500 ml of Dulbecco's modified Eagle medium (growth medium) containing 10% of pre-inactivated fetal calf serum (hereinafter abbreviated as FCS) was charged. 7 × 10 7 seed cells were seeded at 37 ° C. for 4
Culture was started under the condition of 0 rpm. On the third day of growth, the stirring was stopped, the microcarriers with attached cells were allowed to settle, and the culture medium was removed by suction. Fresh growth medium was added and the culture was continued again. On the 4th day of proliferation, the production medium was switched to produce tPA by the same procedure as above. As a medium for production, a Dulbecco's modified Eagle medium containing 20 μM zinc chloride and 10 mM ε-aminocaproic acid was used.
The medium to which various substances shown in (Table 1) were added was used.
After culturing for 2 days, tPA in the culture was quantified by the ELISA method. In addition, microscopic
The degree of cell detachment from the cells was observed. The above results are shown in Table 1.
The results are shown in (Table 1).

【0020】[0020]

【表1】 (注)細胞の剥離(顕微鏡観察) +、++、+++、++++の順に細胞の剥離の程度が
大きい。
[Table 1] (Note) Cell detachment (microscopic observation) The degree of cell detachment is higher in the order of +, ++, ++++, ++++.

【0021】実施例2.実施例1と同じ細胞を使用し
た。pH電極、DO電極及びガス吹き込み管をセットし
た撹拌羽根付きの実容量1l(全容量約1.5l)のベ
ルコ社のスピンナ−フラスコに、マイクロキャリヤ−
(Cytodex1、ファルマシア社)を5gと、予め
不活性化させたFCSを10%含むダルベッコ変法イ−
グル培地(増殖用の培地)を1l仕込んだ。上記の種細
胞を108 個播種し、37℃、30rpm、DO=1〜
2ppm、pH=7.0〜7.2の条件で培養を開始し
た。増殖4日目に、撹拌を停止し、細胞の付着したマイ
クロキャリヤ−を沈降させ、培養液を吸引除去した。新
鮮な増殖用の培地を加え、再び培養を続けた。増殖5日
目に上記同様の操作により、生産培地に切り換え、35
℃の上記同条件でtPAを生産させた。生産用の培地に
は、インシュリン5mg/l、トランスフェリン5mg
/l、塩化亜鉛20μM、ε−アミノカプロン酸10m
Mを含むダルベッコ変法イ−グル培地に、表2(表2)
に示した種々の成分を添加した培地を用いた。以後2日
に一度培地交換を行い、30日間tPAを生産させた。
tPAは、ELISA法により定量し、平均蓄積量、総
蓄積量を産出した。また、生産20日目には顕微鏡によ
りマイクロキャリヤ−からの細胞の剥離の程度を観察し
た。以上の結果を表2(表2)に示した。
Example 2. The same cells as in Example 1 were used. A microcarrier-in a Bellner spinner flask with an actual volume of 1 liter (total volume of about 1.5 liter) equipped with a stirring blade, in which a pH electrode, a DO electrode and a gas blowing tube were set.
(Cytodex 1, Pharmacia) and 5 g of Dulbecco modified method containing 10% of pre-inactivated FCS
1 liter of Glu's medium (medium for growth) was charged. 10 8 seed cells above were seeded, 37 ° C., 30 rpm, DO = 1 to
Cultivation was started under the conditions of 2 ppm and pH = 7.0 to 7.2. On the 4th day of growth, the agitation was stopped, the microcarriers to which the cells were attached were sedimented, and the culture medium was removed by suction. Fresh growth medium was added and the culture was continued again. On the 5th day of growth, the production medium was changed to the production medium by the same operation as above
TPA was produced under the same conditions as above at 0 ° C. Insulin 5mg / l, transferrin 5mg in the production medium
/ L, zinc chloride 20 μM, ε-aminocaproic acid 10 m
Dulbecco's modified Eagle's medium containing M was added to Table 2 (Table 2).
The medium to which the various components shown in 1 above were added was used. After that, the medium was exchanged once every two days to produce tPA for 30 days.
The tPA was quantified by the ELISA method, and the average accumulated amount and the total accumulated amount were produced. On the 20th day of production, the degree of cell detachment from the microcarriers was observed with a microscope. The above results are shown in Table 2 (Table 2).

【0022】[0022]

【表2】 (略号)λCA:λ−カラギ−ナン (注)細胞の剥離(顕微鏡観察) +、++、+++、++++の順に細胞の剥離の程度が
大きい。
[Table 2] (Abbreviation) λCA: λ-carrageenan Note: Cell detachment (microscopic observation) The degree of cell detachment is large in the order of +, ++, ++++, ++++.

【0023】実施例3.浮遊性細胞であり、ヒトモノク
ロ−ナル抗体(以後IgMと略す)を生産するハイブリ
ド−マ、MP5121株(WO90/11350)を使
用した。25cm2の組織培養フラスコに、RPMI1
640培地にFCSを10%加えた培地(増殖用の培
地)を5ml仕込んだ。上記細胞の種細胞を1×105
個/mlとなるように植え込み、37℃の炭酸ガスイン
キュベ−タ−で培養を開始した。増殖3日目に培養液の
全量を抜き出し、遠心分離により培養液を除去し、細胞
を分離した。新鮮な増殖用の培地5mlに細胞を懸濁
し、この細胞懸濁液を25cm2の組織培養フラスコに
戻し、培養を続けた。こうして4日間培養した後、同様
の操作により、増殖用の培地を除去し、生産用の培地に
1×106 個/mlとなるように細胞を懸濁し、細胞懸
濁液の5mlを組織培養フラスコに戻し、37℃で引き
続きIgMの生産を開始した。生産用の培地には、イン
シュリン10mg/l、トランスフェリン10mg/l
を含むRPMI1640培地に、表3(表3)に示した
種々の成分を添加した培地を用いた。以後毎日、前記同
様の方法で生産培地のほぼ全量を回収し、新鮮な生産用
の培地5mlに細胞を懸濁するという操作を繰り返し、
30日間IgMを生産させた。回収した培養液中のIg
MはELISA法で定量し、30日間の総IgM生産量
を算出した。結果を表3(表3)に示した。
Example 3. A hybridoma strain MP5121 (WO90 / 11350), which is a floating cell and produces a human monoclonal antibody (hereinafter abbreviated as IgM), was used. In a 25 cm 2 tissue culture flask, add RPMI1
5 ml of a medium (growth medium) prepared by adding 10% of FCS to 640 medium was charged. 1 × 10 5 seed cells of the above cells
The cells were inoculated so that the number of cells / ml was 1, and the culture was started in a carbon dioxide gas incubator at 37 ° C. On the third day of growth, the whole amount of the culture solution was extracted, the culture solution was removed by centrifugation, and the cells were separated. The cells were suspended in 5 ml of fresh growth medium, the cell suspension was returned to a 25 cm 2 tissue culture flask, and the culture was continued. After culturing for 4 days in this way, the growth medium was removed by the same procedure, and the cells were suspended in the production medium at 1 × 10 6 cells / ml, and 5 ml of the cell suspension was used for tissue culture. The flask was returned to the flask, and the production of IgM was started at 37 ° C. Insulin 10 mg / l, transferrin 10 mg / l
A medium in which various components shown in Table 3 (Table 3) were added to the RPMI1640 medium containing After that, the operation of recovering almost the entire amount of the production medium in the same manner as above and suspending the cells in 5 ml of the fresh production medium was repeated every day.
IgM was produced for 30 days. Ig in the recovered culture solution
M was quantified by the ELISA method and the total IgM production amount for 30 days was calculated. The results are shown in Table 3 (Table 3).

【0024】[0024]

【表3】 [Table 3]

【0025】[0025]

【発明の効果】 本発明においては、付着性細胞、浮遊
性細胞にかかわらず、血清や血清アルブミンを含まない
培地の提供が可能である。即ち、実施例に示したよう
に、培養の比較的困難とされる付着性細胞を適当な培地
で増殖させた後、本発明の無血清培地に切り換えると、
細胞の付着壁からの剥離を抑えることに有効である。さ
らに、本発明の培地で長期に渡って生理活性物質を生産
させると、血清培地と同等以上の生理活性物質の総蓄積
量を示し、動物細胞培養により生理活性物質を安価かつ
大量に生産することに、極めて有効である。
EFFECTS OF THE INVENTION In the present invention, it is possible to provide a medium that does not contain serum or serum albumin regardless of adherent cells or floating cells. That is, as shown in the examples, when the adherent cells, which are relatively difficult to culture, are grown in an appropriate medium and then switched to the serum-free medium of the present invention,
It is effective in suppressing detachment of cells from the adhesion wall. Furthermore, when a physiologically active substance is produced in the medium of the present invention for a long period of time, it shows a total accumulated amount of physiologically active substances which is equal to or higher than that of the serum medium, and it is possible to inexpensively produce a large amount of physiologically active substances by animal cell culture. It is extremely effective.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C12P 21/08 8214−4B //(C12N 9/72 C12R 1:91) (C12P 21/08 C12R 1:91) ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Office reference number FI technical display location C12P 21/08 8214-4B // (C12N 9/72 C12R 1:91) (C12P 21/08 C12R 1:91)

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 λ−カラギ−ナンを含有してなることを
特徴とする、無血清培地。
1. A serum-free medium comprising λ-carrageenan.
【請求項2】 λ−カラギ−ナンの濃度が10〜100
mg/lである、請求項1記載の無血清培地。
2. The concentration of λ-carrageenan is 10 to 100.
The serum-free medium according to claim 1, which is mg / l.
【請求項3】 生理活性物質生産細胞を請求項1、又は
請求項2記載の無血清培地で培養して、生理活性物質を
生産する方法。
3. A method for producing a physiologically active substance by culturing the physiologically active substance-producing cell in the serum-free medium according to claim 1 or 2.
【請求項4】 生理活性物質が組織型プラスミノ−ゲン
活性化因子である、請求項3記載の生理活性物質を生産
する方法。
4. The method for producing a physiologically active substance according to claim 3, wherein the physiologically active substance is a tissue-type plasmin-ogen activator.
【請求項5】 生理活性物質がモノクロ−ナル抗体であ
る、請求項3記載の生理活性物質を生産する方法。
5. The method for producing a physiologically active substance according to claim 3, wherein the physiologically active substance is a monoclonal antibody.
JP4012923A 1992-01-28 1992-01-28 Serumless culture medium Pending JPH05207874A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4012923A JPH05207874A (en) 1992-01-28 1992-01-28 Serumless culture medium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4012923A JPH05207874A (en) 1992-01-28 1992-01-28 Serumless culture medium

Publications (1)

Publication Number Publication Date
JPH05207874A true JPH05207874A (en) 1993-08-20

Family

ID=11818860

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4012923A Pending JPH05207874A (en) 1992-01-28 1992-01-28 Serumless culture medium

Country Status (1)

Country Link
JP (1) JPH05207874A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998000521A1 (en) * 1996-06-28 1998-01-08 The Green Cross Corporation Serum-free media, method for culturing animal cells, and process for producing physiologically active substances
JP2016036342A (en) * 2014-08-07 2016-03-22 株式会社大阪ソーダ Additive for promoting useful substance production
JP2019080526A (en) * 2017-10-31 2019-05-30 株式会社日本バイオセラピー研究所 Method for producing culture supernatant

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998000521A1 (en) * 1996-06-28 1998-01-08 The Green Cross Corporation Serum-free media, method for culturing animal cells, and process for producing physiologically active substances
JP2016036342A (en) * 2014-08-07 2016-03-22 株式会社大阪ソーダ Additive for promoting useful substance production
JP2019080526A (en) * 2017-10-31 2019-05-30 株式会社日本バイオセラピー研究所 Method for producing culture supernatant

Similar Documents

Publication Publication Date Title
US10745672B2 (en) Method of producing a polypeptide or virus of interest in a continuous cell culture
EA023193B1 (en) Cell culture medium for adamts protein expression
JP5719301B2 (en) Method for producing factor VII without serum-free insulin
JP2003506077A5 (en)
Birch et al. Selecting and designing cell lines for improved physiological characteristics
JPH04228066A (en) Culture cell for expressing exogenote
AU2013203993B2 (en) Process for cell culturing by continuous perfusion and alternating tangential flow
JPH05207874A (en) Serumless culture medium
CN103484426B (en) Non-animal source low-protein culture medium
JPH05207875A (en) Serumless culture medium
CA2316739C (en) Preparation of cells for production of biologicals
JPH01101882A (en) Cultivation of mammalian cells
Pörtner et al. Perfusion-microcarrier cultivation of rCHO-cells in serum-free medium for production of human renin
Müthing et al. Microcarrier cultivation of bovine aortic endothelial cells in spinner vessels and a membrane stirred bioreactor
JP6245299B2 (en) Recombinant stable cell clone, its production and its use
JP2011004754A (en) Recombinant stabilized cell clone, production thereof, and use thereof
Chevalot et al. Interest of fed-batch culture for the production of a membrane-bound protein by an adherent animal cell
JPH0728729B2 (en) Method for culturing animal cells
JPH0851993A (en) Production of bioactive substance
JPH07135968A (en) Adhesion of adhesion-independent cell to microcarrier
ARATHOON JOHN R. BIRCH
JP2010099093A (en) Recombinant stable cell clone, and production and use thereof
JP2014223078A (en) Stable recombinant cell clones, production and use thereof