JP2014023541A - Atmosphere-regulating agent and method for culturing cell by using the same - Google Patents

Atmosphere-regulating agent and method for culturing cell by using the same Download PDF

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JP2014023541A
JP2014023541A JP2013230332A JP2013230332A JP2014023541A JP 2014023541 A JP2014023541 A JP 2014023541A JP 2013230332 A JP2013230332 A JP 2013230332A JP 2013230332 A JP2013230332 A JP 2013230332A JP 2014023541 A JP2014023541 A JP 2014023541A
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Shigeki Imagawa
川 茂 樹 今
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Mitsubishi Gas Chemical Co Inc
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Abstract

PROBLEM TO BE SOLVED: To suppress the migration of an aldehyde to a medium, and to reduce the influence to cell culture.SOLUTION: The method for culturing cells comprises the step of placing a culture container housing an atmosphere-regulating agent containing an organic material as a main agent, an aldehyde-removing agent, the cells and the medium in a gas-barrier sealed container, and culturing the cells by regulating the oxygen concentration and the carbon dioxide concentration in the sealed container so as to be 18% or less, and 2% to 10% respectively.

Description

本発明は、雰囲気調整剤およびアルデヒド除去剤を使用した細胞培養方法に関する。   The present invention relates to a cell culture method using an atmosphere adjusting agent and an aldehyde removing agent.

生物、生殖又はバイオテクノロジーの研究分野または産業分野において実施される組織・細胞のような生物試料の培養では大気雰囲気と異なるガス環境が必要とされる。
例えば生細胞観察を長時間連続して行う場合、培養液中の生細胞を通常培養温度で一定に保持するとともに培養液のpHも一定に保持する必要がある。その際、例えば、重炭酸塩緩衝系培養液のpHを血液の通常状態と同じpH7.4に保持するための条件は雰囲気二酸化炭素濃度を5%程度にすることである。
In the culture of biological samples such as tissues and cells carried out in the research field or industrial field of living organisms, reproduction or biotechnology, a gas environment different from the atmospheric environment is required.
For example, when observing living cells continuously for a long time, it is necessary to keep the living cells in the culture solution constant at the normal culture temperature and also to keep the pH of the culture solution constant. At that time, for example, the condition for maintaining the pH of the bicarbonate buffer culture solution at the same pH 7.4 as the normal state of blood is that the atmospheric carbon dioxide concentration is about 5%.

また、多くの研究分野で細胞の低酸素培養が注目されている。具体的には生体内と同様の低酸素雰囲気下で細胞培養を行うことで生体内と同様の生化学反応や血管新生に関連した低酸素誘導因子(HIF)などの遺伝子を誘導したり、細胞の増殖・分化を促進したりする効果が確認されている。また、血流の停止による臓器不全を再現する虚血再灌流実験モデルでも細胞や組織を一定時間無酸素下に置くことで細胞内での機序が詳細に研究されている。さらに、ヒト細胞を用いた薬剤感受性試験では無酸素下で還元雰囲気下を作り出して薬剤代謝試験が実施されている。   In addition, hypoxic culture of cells has attracted attention in many research fields. Specifically, by culturing cells in a hypoxic atmosphere similar to that in vivo, genes such as hypoxia inducing factor (HIF) related to biochemical reactions and angiogenesis similar to those in vivo are induced, Has been confirmed to promote the proliferation and differentiation of the. In addition, in an ischemia reperfusion experimental model that reproduces organ failure due to blood flow cessation, the mechanism in the cell is studied in detail by placing cells and tissues under anoxic for a certain period of time. Furthermore, in a drug sensitivity test using human cells, a drug metabolism test is carried out by creating a reducing atmosphere in the absence of oxygen.

このような生物試料の培養では、所定のガス環境をCOインキュベーターやマルチガスインキュベーターを用いて作成し、その中に入れた通気性のある通常の培養容器で細胞培養を行う。この際、培養容器としては、一般にマルチウェルプレートやフラスコ、シャーレ、チャンバースライド、培養バッグ等が使用される。 In culturing such a biological sample, a predetermined gas environment is created using a CO 2 incubator or a multi-gas incubator, and cell culture is performed in a normal culture vessel having air permeability. In this case, a multiwell plate, a flask, a petri dish, a chamber slide, a culture bag, or the like is generally used as the culture container.

複数の試料を並行して取り扱う場合に異種試料の混入(クロスコンタミネーション:交差汚染)の危険性が常に存在するが、インキュベーター内に多数の試料を共存させることでクロスコンタミネーションの危険性が高まることが懸念されている。そのため複数の試料室を有するインキュベーターが開発されているが、高価につくことから導入できる施設が制限される。また高圧ガスの管理上の問題からインキュベーターの導入が制限されることもある。   When handling multiple samples in parallel, there is always a risk of mixing different types of samples (cross-contamination: cross-contamination), but the risk of cross-contamination increases by having many samples coexist in the incubator. There are concerns. For this reason, an incubator having a plurality of sample chambers has been developed. However, since it is expensive, facilities that can be introduced are limited. In addition, the introduction of incubators may be restricted due to management problems of high-pressure gas.

上記の理由で所定のガス環境を形成するためにインキュベーターに代わって密閉容器とそれに投入する雰囲気調整剤を利用する方法も用いられる。従来、雰囲気調整剤を用いて嫌気・微好気培養する際に、水とホウ酸ナトリウムを主剤とした雰囲気調整剤が多用されてきた。近年安全性と作動の確実性から雰囲気調整剤の主流はアスコルビン酸を主剤とした製品に移行してきている。   For the above reason, in order to form a predetermined gas environment, a method using an airtight container and an atmosphere adjusting agent put in the air in place of the incubator is also used. Conventionally, when an anaerobic / microaerobic culture is performed using an atmosphere adjusting agent, an atmosphere adjusting agent mainly composed of water and sodium borate has been frequently used. In recent years, the mainstream of atmosphere control agents has shifted to products based on ascorbic acid due to safety and operational certainty.

アスコルビン酸類を主剤とした酸素吸収剤は、例えば特許文献1に開示されているようにアスコルビン酸類と金属塩、活性炭及び水を混合して得られる。また特許文献2に開示されているようにアルカリ土類金属水酸化物との混合により発生する炭酸ガスの量、ひいては一定容積の容器内の炭酸ガス濃度をコントロールすることが可能である。特許文献3に記載のように対象とする生物材料に応じて適当な酸素、炭酸ガス濃度を形成しうる雰囲気調整剤が開発され使用されてきた。   An oxygen absorbent mainly composed of ascorbic acids can be obtained by mixing ascorbic acids with a metal salt, activated carbon and water as disclosed in Patent Document 1, for example. Further, as disclosed in Patent Document 2, it is possible to control the amount of carbon dioxide gas generated by mixing with an alkaline earth metal hydroxide, and hence the carbon dioxide concentration in a fixed volume container. As described in Patent Document 3, an atmosphere adjusting agent capable of forming appropriate oxygen and carbon dioxide gas concentrations has been developed and used depending on the target biological material.

有機物を主成分とした雰囲気調整剤は、反応の際に微量な副生成分を発生することがあり、そのような副生成分が対象とする生物種や使用条件によって成育に影響する可能性があることが懸念されていた。   Atmosphere conditioners composed mainly of organic substances may generate a small amount of by-products during the reaction, and such by-products may affect growth depending on the species and conditions of use. There was concern about being there.

特開平10−314581号公報Japanese Patent Laid-Open No. 10-314581 特開平10−327845号公報JP-A-10-327845 特開平09−252766号公報JP 09-252766 A

本発明は上記の雰囲気調整剤を用いた簡易培養技術の上記問題点を解決するため、副生成分の影響を低減する細胞培養方法を提供することを目的とする。   An object of the present invention is to provide a cell culture method that reduces the influence of by-products in order to solve the above-mentioned problems of the simple culture technique using the above-mentioned atmosphere control agent.

本発明者は、鋭意研究を重ねた結果、実際に副生する物質としてアルデヒド類が存在し、放散されるアルデヒドは微量であるが数日間の暴露により水相である培地にアルデヒドが徐々に移行する場合があることを発見し、さらにアルデヒド除去剤を同時に投入することにより培地へのアルデヒドの移行を抑制することが可能であることを見出した。   As a result of extensive research, the present inventor found that aldehydes exist as substances actually produced as by-products, and the amount of aldehyde released is very small, but the aldehyde gradually migrates to the aqueous phase medium after exposure for several days. It was found that it is possible to suppress the transfer of aldehyde to the medium by simultaneously adding an aldehyde remover.

すなわち本発明は、有機物を主剤とする雰囲気調整剤、アルデヒド除去剤並びに細胞及び培地を収容した培養容器を、ガスバリア性密閉容器内に設置し、該密閉容器内の酸素濃度を18%以下、炭酸ガス濃度を2%以上10%以下として細胞を培養することを特徴とする細胞培養方法である。   That is, the present invention provides an atmosphere conditioner mainly composed of an organic substance, an aldehyde remover, and a culture vessel containing cells and a medium in a gas barrier closed vessel, and the oxygen concentration in the closed vessel is 18% or less, carbonic acid. A cell culturing method characterized by culturing cells at a gas concentration of 2% to 10%.

また本発明の細胞培養方法においては、前記有機物が、アスコルビン酸類であること、ガスバリア性密閉容器内に、イオン交換水が収容された開放型の容器がさらに設置され、培養期間中、該イオン交換水中へ移行するアルデヒド濃度が、2.0mg/Lを超えないことが好ましい。   In the cell culture method of the present invention, the organic substance is ascorbic acid, and an open container containing ion-exchanged water is further installed in a gas barrier sealed container, and the ion exchange is performed during the culture period. It is preferred that the concentration of aldehyde that migrates into water does not exceed 2.0 mg / L.

本発明により、アルデヒドに感受性の高い細胞株に対してもクロスコンタミネーションの危険が低減された細胞培養環境を安価な設備で構築することが可能となった。   According to the present invention, it has become possible to construct a cell culture environment in which the risk of cross-contamination is reduced even with a cell line that is highly sensitive to aldehyde, with inexpensive equipment.

本発明における雰囲気調整剤とは、大気下で酸素と化学反応することにより、ガスバリア性密閉容器内の酸素濃度及び炭酸ガス濃度を対象とする細胞の成育に適した特定の範囲、例えば酸素濃度を18%以下、炭酸ガス濃度を2%以上10%以下に調整させ得るものである。本発明の雰囲気調整剤は、酸素吸収反応の主剤となる有機物の他、水、多孔質担体及び金属化合物を含有し、さらに、反応場の制御を目的として炭酸塩またはアルカリ土類金属水酸化物を含有する。   The atmospheric conditioner in the present invention is a specific range suitable for the growth of cells targeting the oxygen concentration and carbon dioxide concentration in the gas barrier closed container by chemically reacting with oxygen in the atmosphere, for example, oxygen concentration. The carbon dioxide gas concentration can be adjusted to 18% or less and 2% or more and 10% or less. The atmosphere conditioner of the present invention contains water, a porous carrier and a metal compound in addition to an organic substance which is a main component of the oxygen absorption reaction, and further, carbonate or alkaline earth metal hydroxide for the purpose of controlling the reaction field. Containing.

酸素吸収反応の主剤としては炭酸ガス発生能を併せ持つ有機物が用いられ、中でもアスコルビン酸類が有効である。   As the main component of the oxygen absorption reaction, an organic substance having a carbon dioxide generating ability is used, and ascorbic acids are particularly effective.

アスコルビン酸類を主剤とした場合には、L−アスコルビン酸、L−アスコルビン酸ナトリウム、L−アスコルビン酸カルシウム、D−iso−アスコルビン酸ナトリウムの単体もしくはこれらの混合物が用いられる。これらアスコルビン酸類は水溶液として活性炭等の多孔質担体に含浸させて用いることが好ましい。アスコルビン酸塩の水溶液は濃度の濃い方が多孔質担体の使用量を少なくすることができるため、アスコルビン酸類の濃度は、できるだけ飽和溶解度に近い濃度にすることが好ましい。また、酸素吸収反応に必要な水分量はアスコルビン酸類の水溶液を用いることによって充分確保される。このためアスコルビン酸類は溶解度の高い塩が好ましく、具体的にはL−アスコルビン酸ナトリウムが好ましい。L−アスコルビン酸ナトリウムを使用した場合、該水溶液の濃度を40〜55重量%とすることが好適である。   When ascorbic acid is used as the main agent, L-ascorbic acid, L-sodium ascorbate, calcium L-ascorbate, sodium D-iso-sodium ascorbate or a mixture thereof is used. These ascorbic acids are preferably used by impregnating a porous carrier such as activated carbon as an aqueous solution. As the concentration of the ascorbate aqueous solution is higher, the amount of the porous carrier used can be reduced. Therefore, the concentration of ascorbic acid is preferably as close to the saturation solubility as possible. Further, the amount of water necessary for the oxygen absorption reaction is sufficiently ensured by using an aqueous solution of ascorbic acids. For this reason, ascorbic acids are preferably highly soluble salts, specifically sodium L-ascorbate. When sodium L-ascorbate is used, the concentration of the aqueous solution is preferably 40 to 55% by weight.

多孔質担体としては、活性炭の他、珪藻土、シリカゲル、ゼオライト、パーライト、珪酸カルシウム、軽石、セルロース、活性白土、アルミナ、ヒドロキシアパタイト、多孔質樹脂、多孔質ガラス等が例示できる。活性炭を用いる場合、おが粉、石炭、椰子殻等を原料として水蒸気賦活、炭酸ガス賦活等の各種製法で製造された活性炭を用いることができる。また活性炭は、アスコルビン酸類等を水溶液として活性炭に担持させ顆粒状で小袋に充填して用いられるために、粒状活性炭が好ましい。粒状活性炭の粒子径は、好ましくは0.1mm〜2mm、より好ましくは0.5〜1mmである。粒状活性炭の粒子径は上記範囲より細かくなると、雰囲気調整剤の流動性が悪くなり自動充填が困難となる。また、粒子径が大きすぎると酸素吸収性能が低下したり、包装体を突き破り、内容物がこぼれ出したりという問題が生じる。   Examples of the porous carrier include activated carbon, diatomaceous earth, silica gel, zeolite, pearlite, calcium silicate, pumice, cellulose, activated clay, alumina, hydroxyapatite, porous resin, porous glass, and the like. When activated carbon is used, activated carbon produced by various production methods such as steam activation and carbon dioxide activation using sawdust, coal, coconut shell and the like as raw materials can be used. The activated carbon is preferably granular activated carbon because it is used as an ascorbic acid or the like as an aqueous solution supported on the activated carbon and filled in a small bag. The particle diameter of the granular activated carbon is preferably 0.1 mm to 2 mm, more preferably 0.5 to 1 mm. If the particle diameter of the granular activated carbon is finer than the above range, the fluidity of the atmosphere modifier becomes poor and automatic filling becomes difficult. In addition, if the particle size is too large, there are problems that the oxygen absorption performance is lowered, the package is broken, and the contents spill out.

本発明の細胞培養方法で用いられる雰囲気調整剤には、酸素吸収反応に対して触媒作用を有する金属化合物が加えられる。金属化合物としては、塩化第1鉄、塩化第2鉄、硫酸第1鉄、硫酸第2鉄、塩化マンガン、硫酸亜鉛、硫酸銅、塩化銅の無水塩又は含水塩が好ましい。金属化合物の配合量は、アスコルビン酸類100重量部に対し金属化合物5〜20重量部が好ましい。   The atmosphere adjusting agent used in the cell culture method of the present invention is added with a metal compound having a catalytic action for the oxygen absorption reaction. As the metal compound, ferrous chloride, ferric chloride, ferrous sulfate, ferric sulfate, manganese chloride, zinc sulfate, copper sulfate, an anhydrous salt or hydrated salt of copper chloride is preferable. As for the compounding quantity of a metal compound, 5-20 weight part of metal compounds are preferable with respect to 100 weight part of ascorbic acids.

本発明の細胞培養方法で用いられる雰囲気調整剤においては、反応を迅速に進行させるため、反応場をアルカリ領域に制御する炭酸塩を加えることができる。炭酸塩としては、炭酸ナトリウム、炭酸水素ナトリウム、炭酸ナトリウムの水和物等水溶性の炭酸塩が好ましい。炭酸塩の配合量は、アスコルビン酸類100重量部に対し炭酸塩10〜30重量部が好ましい。   In the atmosphere adjusting agent used in the cell culture method of the present invention, a carbonate for controlling the reaction field in the alkaline region can be added in order to rapidly advance the reaction. The carbonate is preferably a water-soluble carbonate such as sodium carbonate, sodium bicarbonate, sodium carbonate hydrate. As for the compounding quantity of carbonate, 10-30 weight part of carbonate is preferable with respect to 100 weight part of ascorbic acids.

本発明の細胞培養方法で用いられる雰囲気調整剤においては、炭酸ガス濃度を制御するため、上記の炭酸塩に代えて炭酸ガス吸収剤としてアルカリ土類金属水酸化物が使用されることがある。特に水酸化カルシウム、水酸化マグネシウムまたはこれらの混合物が好適に用いられる。アルカリ土類金属水酸化物は、平均粒径1〜100μmの粉体が好ましく用いられ、平均粒径が2〜50μmの粉体がより好ましく用いられる。アルカリ土類金属水酸化物の配合量は、活性炭にアスコルビン酸類、金属塩及び水を含浸させた雰囲気調整剤100重量部に対して5〜25重量部が必要である。この量より少ない場合酸素吸収及び炭酸ガス発生が迅速に行われない。また配合量が多すぎると炭酸ガス濃度が低くなりすぎるばかりでなく、酸素吸収速度の低下につながり雰囲気調整剤を多量に要することになる。   In the atmosphere adjusting agent used in the cell culture method of the present invention, an alkaline earth metal hydroxide may be used as a carbon dioxide absorbent instead of the above carbonate in order to control the carbon dioxide concentration. In particular, calcium hydroxide, magnesium hydroxide or a mixture thereof is preferably used. As the alkaline earth metal hydroxide, a powder having an average particle diameter of 1 to 100 μm is preferably used, and a powder having an average particle diameter of 2 to 50 μm is more preferably used. The blending amount of the alkaline earth metal hydroxide is required to be 5 to 25 parts by weight with respect to 100 parts by weight of the atmosphere modifier obtained by impregnating activated carbon with ascorbic acid, metal salt and water. When the amount is less than this amount, oxygen absorption and carbon dioxide generation are not performed rapidly. Moreover, when there are too many compounding quantities, a carbon dioxide gas density | concentration will become low too much, and it will lead to the fall of an oxygen absorption rate, and will require a lot of atmosphere regulators.

これらの成分は固体のまま配合若しくは水溶液として活性炭、珪藻土、ゼオライト等の多孔質担体に担持されて用いられるが、放出されたアルデヒドの再吸着効果を有する後者の形態がより好適に用いられる。   These components are blended as solids or used as an aqueous solution and supported on a porous carrier such as activated carbon, diatomaceous earth, or zeolite. The latter form having the effect of resorbing released aldehyde is more preferably used.

この他、酸素吸収反応の進行に伴う、雰囲気調整剤の過度の発熱を抑制するために、雰囲気調整剤に対して熱可塑性樹脂の粒状体を配合することが好ましい。使用される熱可塑性樹脂は1〜500μmの粒子系が好ましく、10〜300μmのものがより好ましい。熱可塑性樹脂の軟化点は90〜125℃が好ましく、種類に特に制限はないがポリエチレン、ポリプロピレン、エチレン−酢酸ビニル共重合体、エラストマー、又はこれらの混合物が使用できるが、特に分子量10000以下の低分子量ポリエチレン、ポリプロピレンまたはこれらの混合物が好適に用いられる。軟化点が低すぎると雰囲気調整剤の正常な反応を阻害する一方、軟化点が高すぎると雰囲気調整剤の過度の発熱を抑制することができない。   In addition, in order to suppress excessive heat generation of the atmosphere adjusting agent accompanying the progress of the oxygen absorption reaction, it is preferable to blend a thermoplastic resin granule with the atmosphere adjusting agent. The thermoplastic resin used preferably has a particle system of 1 to 500 μm, more preferably 10 to 300 μm. The softening point of the thermoplastic resin is preferably 90 to 125 ° C., and the type is not particularly limited, but polyethylene, polypropylene, ethylene-vinyl acetate copolymer, elastomer, or a mixture thereof can be used. Molecular weight polyethylene, polypropylene or a mixture thereof is preferably used. If the softening point is too low, the normal reaction of the atmosphere adjusting agent is inhibited. On the other hand, if the softening point is too high, excessive heat generation of the atmosphere adjusting agent cannot be suppressed.

これらの雰囲気調整剤は、通気性を有する包装材料に収納される。通気性包材は、酸素と炭酸ガスを透過するものであれば良く、酸素透気度300mL/(h・m)以上かつ炭酸ガス透気度が300mL/(h・m)以上の包材が好ましい。包装材料としてはたとえば紙、不織布、有孔フィルムおよびそれらの積層物が用いられる。 These atmosphere adjusting agents are accommodated in a packaging material having air permeability. The breathable wrapping material only needs to be permeable to oxygen and carbon dioxide gas, and has a gas permeability of 300 mL / (h · m 2 ) or more and a carbon dioxide gas permeability of 300 mL / (h · m 2 ) or more. A material is preferred. As the packaging material, for example, paper, non-woven fabric, perforated film and laminates thereof are used.

上記の雰囲気調整剤包装体はその機能を長期間維持するため、使用前はガスバリア性の容器や袋に収納されており、使用するにあたりガスバリア性の容器や袋から取り出して用いられる。   In order to maintain the function for a long period of time, the above-described atmosphere modifier package is stored in a gas-barrier container or bag before use, and is taken out from the gas-barrier container or bag before use.

本発明の細胞培養方法で使用されるアルデヒド除去剤は、常温でアルデヒド類と反応しうる化合物を主剤として構成される。このような化合物として、アミン類、アミド類、イミド類、アミノ酸類、ヒドラジン誘導体、過酸化物の他、鉱物セピオライトの様なアルデヒド吸収能を有する天然物、活性炭等の吸着剤、パラジウムのような金属触媒、アルデヒド分解能を有する酵素類などから選択され、これらを単独もしくは混合して用いることができる。なかでも、アミン類、ヒドラジン誘導体等が好適に用いられ、エチレン尿素、スルファニル酸、アミノグアニジン等が特に好適に用いられる。   The aldehyde removing agent used in the cell culture method of the present invention is composed mainly of a compound that can react with aldehydes at room temperature. Examples of such compounds include amines, amides, imides, amino acids, hydrazine derivatives, peroxides, natural products having an aldehyde absorption ability such as mineral sepiolite, adsorbents such as activated carbon, and palladium. It is selected from metal catalysts, enzymes having aldehyde resolution, and the like, and these can be used alone or in combination. Of these, amines, hydrazine derivatives and the like are preferably used, and ethylene urea, sulfanilic acid, aminoguanidine and the like are particularly preferably used.

アルデヒド除去剤には、主剤の他、主剤とアルデヒド類の反応を妨げない範囲で、主剤を担持させる多孔質担体や流動性を向上させる分散剤などを添加しても構わない。多孔質担体としては雰囲気調整剤に使用されるものと同じものを用いることができるが、アルデヒド吸着能を有する活性炭が好ましく用いられる。   In addition to the main agent, a porous carrier for supporting the main agent and a dispersant for improving fluidity may be added to the aldehyde removing agent as long as the reaction between the main agent and aldehydes is not hindered. The same porous carrier as that used for the atmosphere adjusting agent can be used, but activated carbon having an aldehyde adsorption ability is preferably used.

ガスバリア性密閉容器内にアルデヒド除去剤を投入する方法としては、アルデヒド除去剤を充填した包装体を雰囲気調整剤とは別個の包装体として投入する方法の他、雰囲気調整剤に直接配合する方法、多孔質担体に担持させて雰囲気調整剤と混合する方法のいずれを選択しても良い。系内で必要とされるアルデヒド除去剤の量は、目的とする細胞や培養容器の形状、容積、数量により異なるが、ガスバリア性密閉容器内に設置された開放型の容器内に収容したイオン交換水へ、培養期間中に移行するアルデヒドの濃度が、2.0mg/L、好ましくは1.6mg/Lを超えない様に使用量を設定することが好ましい。   As a method for introducing the aldehyde remover into the gas barrier closed container, in addition to a method of introducing the package filled with the aldehyde remover as a separate package from the atmosphere modifier, a method of directly blending in the atmosphere modifier, Any method may be selected which is supported on a porous carrier and mixed with an atmosphere adjusting agent. The amount of aldehyde removal agent required in the system varies depending on the shape, volume, and quantity of the target cells and culture vessel, but ion exchange accommodated in an open container installed in a gas barrier closed container. It is preferable to set the usage amount so that the concentration of aldehyde transferred to water during the culture period does not exceed 2.0 mg / L, preferably 1.6 mg / L.

本発明の細胞培養方法によれば、予めガスバリア性密閉容器内にアルデヒド除去剤を同梱することにより、副生するアルデヒド類の培地への移行を抑制することで細胞への悪影響を回避することができる。   According to the cell culture method of the present invention, an aldehyde remover is bundled in advance in a gas barrier closed container, thereby avoiding adverse effects on cells by suppressing the transfer of by-product aldehydes to the medium. Can do.

本発明の細胞培養方法で用いられるガスバリア性密閉容器は、その内外の気体の流通を妨げ、投入した雰囲気調整剤により形成された酸素、炭酸ガス濃度を長期間保持するものである。ガラス、金属、ポリカーボネート等で構成された容器が良く用いられるが、ガスバリア性フィルム及びその積層物を使用することも可能である。   The gas barrier closed container used in the cell culturing method of the present invention prevents the flow of gas inside and outside thereof, and maintains the oxygen and carbon dioxide gas concentrations formed by the introduced atmosphere adjusting agent for a long period of time. A container made of glass, metal, polycarbonate or the like is often used, but a gas barrier film and a laminate thereof can also be used.

本発明の細胞培養方法で用いられる培養容器は、容器外との通気性が確保されていれば特に制限はなく、容積、形状、材質等いずれも培養に適した任意のものを採用することができる。また、蓋部を有する培養容器が好ましく用いられるが、この際も、容器外との通気性を確保する必要がある。   The culture vessel used in the cell culturing method of the present invention is not particularly limited as long as air permeability to the outside of the vessel is ensured, and any volume, shape, material, etc. suitable for culture can be adopted. it can. Moreover, although the culture container which has a cover part is used preferably, it is necessary to ensure the air permeability with the outside of a container also in this case.

本発明の細胞培養方法で用いられる培地に特に制限はなく、一般的に使用されているものがそのまま適用できるため、培養する細胞に適した培地を自由に選択できる。   There is no restriction | limiting in particular in the culture medium used with the cell culture method of this invention, Since what is generally used can be applied as it is, the culture medium suitable for the cell to culture | cultivate can be selected freely.

本発明の細胞培養方法は、細胞及び培地を収容した培養容器と共に、有機物を主剤とする雰囲気調整剤及びアルデヒド除去剤、或いはアルデヒド除去剤が配合された有機物を主剤とする雰囲気調整剤を、ガスバリア性密閉容器内に設置後、密封し、該密閉容器を細胞培養に好適な温度下に静置することで実施できる。この際、ガスバリア性密閉容器内で発生したアルデヒドの発生量を測定する目的で、該密閉容器内にイオン交換水を収容した開放型の容器を設置しても構わない。開放型の容器としては培養容器の他、ビーカー、フラスコなどが例示でき、細胞及び培地を収容した培養容器と同型の培養容器であることが好ましい。   The cell culturing method of the present invention includes a culture vessel containing cells and a medium, and an atmosphere conditioner and aldehyde remover mainly composed of an organic substance, or an atmosphere conditioner mainly composed of an organic substance containing an aldehyde remover and a gas barrier. This can be carried out by placing it in an airtight container, sealing it, and allowing the container to stand at a temperature suitable for cell culture. At this time, for the purpose of measuring the amount of aldehyde generated in the gas barrier sealed container, an open container containing ion-exchanged water may be installed in the sealed container. Examples of the open type container include a beaker, a flask and the like in addition to the culture container, and the culture container is preferably the same type as the culture container containing the cells and the medium.

細胞及び培地を培養容器に収容する方法としては、予め細胞を播種した培地を培養容器に収容する方法や、培養容器に培地のみを収容した後、培地に対して細胞を播種する方法など、使用する細胞や培地の種類に応じて任意の方法を採用することができる。   As a method for accommodating cells and culture medium in a culture container, a method of accommodating a culture medium in which cells are seeded in advance in a culture container or a method of seeding cells in a culture medium after storing only the culture medium in the culture container is used Any method can be employed depending on the type of cells and medium to be used.

以下に実施例をあげて本願発明を詳細に説明するが、本願発明はこれによって限定されるものではない。   Hereinafter, the present invention will be described in detail with reference to examples, but the present invention is not limited thereto.

以下の実施例・比較例・参考例では下記に示す「細胞」、「培地」、「培養容器」をそれぞれ使用した。
1.細胞
ヒト腎臓由来細胞(Tig−3−20:ヒューマンサイエンス振興財団研究資源バンクより分譲 資源番号JCRB0506 ロット番号R034)
2.培地
MEM培地(製品名;GIBCO社製 11095−080(MEM Earle’s liquid))
3.培養容器
60mm径ディッシュ(製品名;AGCテクノグラス社製 IWAKI3010−060 60mm/Tissue Culture Dish)
In the following Examples, Comparative Examples, and Reference Examples, “cells”, “medium”, and “culture vessel” shown below were used.
1. Cells Human kidney-derived cells (Tig-3-20: Sold by Human Science Foundation Research Resource Bank resource number JCRB0506 lot number R034)
2. Medium MEM medium (product name: 11095-080 (MEM Earle's liquid) manufactured by GIBCO)
3. Cultivation container 60 mm diameter dish (Product name: IWAKI 3010-060 60 mm / Tissue Culture Dish manufactured by AGC Techno Glass)

(実施例1)
L−アスコルビン酸ナトリウム水溶液(濃度45重量%)100gに硫酸第一鉄・7水塩6g及びアルデヒド除去剤であるエチレン尿素0.3gを溶解させ、水溶液を顆粒状活性炭(平均粒径0.6mm)60gに含浸させた後、低分子量ポリエチレン70g及び炭酸ナトリウム・10水塩20gを添加混合してアルデヒド除去剤が配合された酸素吸収・炭酸ガス発生剤(A)を得た。
Example 1
In 100 g of an aqueous solution of sodium L-ascorbate (concentration 45% by weight), 6 g of ferrous sulfate and heptahydrate and 0.3 g of ethylene urea as an aldehyde removing agent were dissolved, and the aqueous solution was made into granular activated carbon (average particle size 0.6 mm). ) After impregnating 60 g, 70 g of low molecular weight polyethylene and 20 g of sodium carbonate · 10 hydrate were added and mixed to obtain an oxygen absorption / carbon dioxide gas generator (A) containing an aldehyde remover.

有孔ポリエチレンフィルムでラミネートした和紙の縦90mm×横55mm通気性小袋に(A)を5g充填してアルデヒド除去剤が配合された酸素吸収・炭酸ガス発生包装体(A’)とした。   An oxygen-absorbing / carbon dioxide generating package (A ') in which 5 g of (A) was filled in a breathable sachet of 90 mm long by 55 mm wide laminated with perforated polyethylene film was blended with an aldehyde remover.

アルデヒド除去剤が配合された酸素吸収・炭酸ガス発生包装体(A’)と1.0×10個/mLまたは5.0×10個/mLの細胞密度でヒト腎臓由来細胞を播種した10%牛胎児血清(以下、FBSと表記する)添加MEM培地5mL入り60mm径ディッシュ各2枚を、イオン交換水5mL入り60mm径ディッシュ2枚と共に容積2500mLのポリカーボネート製ガスバリア性密閉容器に装填した。37℃で3日間培養した後、細胞数を測定し、イオン交換水に移行したアルデヒド濃度をMBTH法(3−メチル−2−ベンゾチアゾリノンヒドラゾン比色法、(株)共立理化学研究所 アルデヒド測定試薬LR−FOR)にて測定した。それら結果を、細胞培養後の密閉容器内の酸素濃度及び炭酸ガス濃度と共に表1に記載する。表1から、培養後の細胞数が10倍以上に増加したことが認められる。 Oxygen absorption / carbon dioxide generating package (A ′) containing an aldehyde removing agent and human kidney-derived cells were seeded at a cell density of 1.0 × 10 4 cells / mL or 5.0 × 10 3 cells / mL. Two 60 mm diameter dishes each containing 5 mL of MEM medium supplemented with 10% fetal bovine serum (hereinafter referred to as FBS) were loaded together with two 60 mm diameter dishes containing 5 mL of ion-exchanged water into a 2500 mL polycarbonate gas barrier sealed container. After culturing at 37 ° C. for 3 days, the number of cells was measured, and the aldehyde concentration transferred to ion-exchanged water was determined by the MBTH method (3-methyl-2-benzothiazolinone hydrazone colorimetric method, Kyoritsu Riken Laboratories, Inc. Measurement was performed with a measuring reagent LR-FOR). The results are shown in Table 1 together with the oxygen concentration and carbon dioxide concentration in the sealed container after cell culture. From Table 1, it can be seen that the number of cells after culture increased more than 10 times.

(実施例2)
L−アスコルビン酸ナトリウム水溶液(濃度45重量%)100gに硫酸第一鉄・7水塩6g及び炭酸ナトリウム・10水塩20gを溶解させ、水溶液を顆粒状活性炭(平均粒径0.6mm)60gに含浸させ、低分子量ポリエチレン70gを添加混合して酸素吸収・炭酸ガス発生剤(B)を得た。
(Example 2)
In 100 g of sodium L-ascorbate aqueous solution (concentration 45% by weight), 6 g of ferrous sulfate and heptahydrate and 20 g of sodium carbonate and 10 hydrate are dissolved, and the aqueous solution is made into 60 g of granular activated carbon (average particle size 0.6 mm). It was impregnated, and 70 g of low molecular weight polyethylene was added and mixed to obtain an oxygen absorbing / carbon dioxide generating agent (B).

有孔ポリエチレンフィルムでラミネートした和紙の縦通気性小袋90mm×横55mmに(B)を5g充填して酸素吸収・炭酸ガス発生包装体(B’)とした。   5 g of (B) was filled into a 90 mm long x 55 mm wide Japanese paper longitudinally breathable sachet laminated with a perforated polyethylene film to obtain an oxygen absorbing / carbon dioxide generating package (B ′).

市販の低級アルデヒド吸着剤アルデナイト(日本エンバイロケミカルズ株式会社製アルデヒド吸着剤 以下アルデナイト)2.0gを有孔ポリエチレンフィルムでラミネートした和紙の通気性小袋縦90mm×横55mmに充填してアルデヒド除去包装体(C)とした。   Aldenite (alkaline aldehyde adsorbent manufactured by Nippon Enviro Chemicals Co., Ltd.) 2.0g of commercially available lower aldehyde adsorbent, filled with perforated polyethylene film, filled into a breathable sachet of 90mm x 55mm in width to remove aldehyde Body (C).

酸素吸収・炭酸ガス発生包装体(B’)及びアルデヒド除去包装体(C)と、1.0×10個/mLまたは5.0×10個/mLの細胞密度でヒト腎臓由来細胞を播種した10%FBS添加MEM培地5mL入り60mm径ディッシュ各2枚を、イオン交換水5mL入り60mm径ディッシュ2枚と共に容積2500mLのポリカーボネート製ガスバリア性密閉容器に装填した。37℃で3日間培養した後、細胞数を測定し、イオン交換水に移行したアルデヒド濃度をMBTH法にて測定した。それら結果を、細胞培養後の密閉容器内の酸素濃度及び炭酸ガス濃度と共に表1に記載する。表1から、培養後の細胞数が10倍以上に増加したことが認められる。 Oxygen absorption / carbon dioxide generation package (B ′) and aldehyde removal package (C), and human kidney-derived cells at a cell density of 1.0 × 10 4 cells / mL or 5.0 × 10 3 cells / mL Two 60 mm-diameter dishes each containing 5 mL of 10% FBS-added MEM medium sowed together with two 60-mm diameter dishes containing 5 mL of ion-exchanged water were loaded into a 2500-mL polycarbonate gas barrier sealed container. After culturing at 37 ° C. for 3 days, the number of cells was measured, and the concentration of aldehyde transferred to ion-exchanged water was measured by the MBTH method. The results are shown in Table 1 together with the oxygen concentration and carbon dioxide concentration in the sealed container after cell culture. From Table 1, it can be seen that the number of cells after culture increased more than 10 times.

(比較例1)
有孔ポリエチレンフィルムでラミネートした和紙の通気性小袋90mm×横55mmに実施例2で得られた酸素吸収・炭酸ガス発生剤(B)を5g充填して酸素吸収・炭酸ガス発生包装体(B’)とした。
(Comparative Example 1)
An oxygen absorbing / carbon dioxide generating package (B ′) obtained by filling 5 g of the oxygen absorbing / carbon dioxide generating agent (B) obtained in Example 2 into a 90 mm × 55 mm wide Japanese paper breathable sachet laminated with a perforated polyethylene film. ).

酸素吸収・炭酸ガス発生包装体(B’)と1.0×10個/mLまたは5.0×10個/mLの細胞密度でヒト腎臓由来細胞を播種した10%FBS添加MEM培地5mL入り60mm径ディッシュ各2枚を、イオン交換水5mL入り60mm径ディッシュ2枚と共に容積2500mLのポリカーボネート製ガスバリア性密閉容器に装填した。37℃で3日間培養した後、細胞数を測定し、イオン交換水に移行したアルデヒド濃度をMBTH法にて測定した。その結果を、細胞培養後の密閉容器内の酸素濃度及び炭酸ガス濃度と共に表1に記載する。アルデヒド除去剤を使用せず細胞を培養した結果、細胞数の増加は2〜5倍程度に留まった。 Oxygen-absorbing / carbon dioxide generating package (B ′) and 5% 10% FBS-added MEM medium seeded with human kidney-derived cells at a cell density of 1.0 × 10 4 cells / mL or 5.0 × 10 3 cells / mL Two pieces each containing 60 mm diameter dishes were loaded together with two 60 mm diameter dishes containing 5 mL of ion exchange water into a polycarbonate gas barrier hermetically sealed container having a volume of 2500 mL. After culturing at 37 ° C. for 3 days, the number of cells was measured, and the concentration of aldehyde transferred to ion-exchanged water was measured by the MBTH method. The results are shown in Table 1 together with the oxygen concentration and carbon dioxide concentration in the sealed container after cell culture. As a result of culturing the cells without using an aldehyde remover, the increase in the number of cells remained about 2 to 5 times.

(参考例1)
1.0×10個/mLまたは5.0×10個/mLの細胞密度でヒト腎臓由来細胞を播種した10%FBS添加MEM培地5mL入り60mm径ディッシュ各2枚を、イオン交換水5mL入り60mm径ディッシュ2枚と共に酸素18%炭酸ガス5%に設定したマルチガスインキュベーターに装填し、37℃で3日間培養した後、細胞数を計測した。それら結果を表1に記載する。アルデヒドの発生源である酸素吸収・炭酸ガス発生包装体を使用せず、マルチガスインキュベーターを使用して細胞を培養した結果、アルデヒド除去剤を併用した実施例1及び2と同程度の細胞数の増加が見られた。
(Reference Example 1)
Two 60 mm diameter dishes each containing 5 mL of 10% FBS-added MEM medium seeded with human kidney-derived cells at a cell density of 1.0 × 10 4 cells / mL or 5.0 × 10 3 cells / mL were added to 5 mL of ion-exchanged water. The sample was loaded into a multi-gas incubator set to oxygen 18% carbon dioxide gas 5% together with two 60 mm diameter dishes and cultured for 3 days at 37 ° C., and the number of cells was counted. The results are listed in Table 1. As a result of culturing cells using a multi-gas incubator without using an oxygen absorption / carbon dioxide generating package that is an aldehyde generation source, the number of cells was about the same as in Examples 1 and 2 combined with an aldehyde remover. An increase was seen.

Figure 2014023541
Figure 2014023541

有機物を主剤とする雰囲気調整剤とアルデヒド除去剤を併用する本発明の細胞培養方法は、マルチガスインキュベーターを使用した場合と同等の細胞培養結果を得ることができる、簡便且つ経済的な細胞培養方法である。   The cell culture method of the present invention using an organic substance-based atmosphere modifier and an aldehyde remover in combination is a simple and economical cell culture method capable of obtaining the same cell culture results as when a multi-gas incubator is used. It is.

Claims (3)

有機物を主剤とする雰囲気調整剤、アルデヒド除去剤並びに細胞及び培地を収容した培養容器を、ガスバリア性密閉容器内に設置し、該密閉容器内の酸素濃度を18%以下、炭酸ガス濃度を2%以上10%以下として細胞を培養することを特徴とする細胞培養方法。   A culture vessel containing an atmosphere conditioner mainly composed of organic substances, an aldehyde removing agent, cells and a medium is placed in a gas barrier sealed container, and the oxygen concentration in the sealed container is 18% or less and the carbon dioxide gas concentration is 2%. A cell culture method comprising culturing cells at 10% or less. 前記有機物が、アスコルビン酸類である、請求項1記載の細胞培養方法。   The cell culture method according to claim 1, wherein the organic substance is ascorbic acid. ガスバリア性密閉容器内に、イオン交換水が収容された開放型の容器がさらに設置され、培養期間中に該イオン交換水中へ移行するアルデヒド濃度が、2.0mg/Lを超えない請求項1または2記載の細胞培養方法。   An open container containing ion-exchanged water is further installed in the gas barrier closed container, and the concentration of aldehyde transferred to the ion-exchanged water during the culture period does not exceed 2.0 mg / L. 2. The cell culture method according to 2.
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JPH09252766A (en) * 1996-03-26 1997-09-30 Mitsubishi Gas Chem Co Inc Agent for controlling concentration of gas and method for controlling low oxygen-concentration environment
JPH10327845A (en) * 1997-04-01 1998-12-15 Mitsubishi Gas Chem Co Inc Atmoshohere adjusting agent and culture of anaerobic bacterium
JP2004148221A (en) * 2002-10-31 2004-05-27 Nippon Synthetic Chem Ind Co Ltd:The Aldehyde adsorbent and its application

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