JP4378514B2 - Cell culture vessel - Google Patents

Cell culture vessel Download PDF

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JP4378514B2
JP4378514B2 JP2003344093A JP2003344093A JP4378514B2 JP 4378514 B2 JP4378514 B2 JP 4378514B2 JP 2003344093 A JP2003344093 A JP 2003344093A JP 2003344093 A JP2003344093 A JP 2003344093A JP 4378514 B2 JP4378514 B2 JP 4378514B2
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culture
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aqueous solution
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solution
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JP2005102657A (en
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宗夫 高沖
淳一郎 行徳
睦 永瀬
登 安藤
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Japan Aerospace Exploration Agency JAXA
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M23/00Constructional details, e.g. recesses, hinges
    • C12M23/24Gas permeable parts
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M23/00Constructional details, e.g. recesses, hinges
    • C12M23/02Form or structure of the vessel
    • C12M23/04Flat or tray type, drawers
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M23/00Constructional details, e.g. recesses, hinges
    • C12M23/38Caps; Covers; Plugs; Pouring means

Description

本発明は、微小重力下において動物細胞等の細胞を培養試験する際に用いて好適な細胞培養容器に関するものである。   The present invention relates to a cell culture vessel suitable for use in culturing cells such as animal cells under microgravity.

宇宙空間のような微小重力下で動物細胞の培養試験を行なう場合には、何等かの方法によって上記動物細胞に酸素を供給する必要がある。ところが、周知のように、上記微小重力下においては、気液が実質的に二層分離することが無いために、地上におけるような気液が二層分離した状態での静置観測による試験を行なうことができない。そこで、一般に微小重力下において動物細胞の培養試験を行なうに際しては、培養容器内に満液状態に培養液を充填するとともに、外部から連続的にあるいは間欠的に、所定の酸素を含有する新たな培養液を循環供給する方法が採用されている。   When performing animal cell culture tests under microgravity such as in outer space, it is necessary to supply oxygen to the animal cells by some method. However, as is well known, under the above-mentioned microgravity, the gas-liquid is not substantially separated into two layers. I can't do it. Therefore, in general, when performing an animal cell culture test under microgravity, the culture vessel is filled with the culture solution in a full state, and a new oxygen-containing solution is continuously or intermittently added from the outside. A method of circulating and supplying the culture solution is employed.

しかしながら、上記培養容器において、培養液中の酸素濃度を一定範囲に保持するためには、比較的頻繁に培養液を交換する必要があり、そのためには培養液循環ポンプや酸素供給用の設備を外部に別途設置する必要があることから、特に極力狭い空間での試験の実施が要請される宇宙空間にあっては、実施上の制約が大きくなるという問題点があった。   However, in order to maintain the oxygen concentration in the culture solution within a certain range in the culture vessel, it is necessary to replace the culture solution relatively frequently. For this purpose, a culture solution circulation pump and an oxygen supply facility are required. Since it is necessary to install it separately outside, there is a problem that the restriction on the implementation becomes large especially in the space where the execution of the test in the narrowest space is required.

そこで、本発明者等は、先に、上記問題点を解消するために、図3に示すように、両面間に貫通して培養液が充填される空間部1Aが形成された板状の本体1と、この本体1の一方の面に配設されて上記空間部1Aを塞ぐとともに上記空間部1A側の表面が細胞付着性を有する培養板2と、上記本体1の他方の面に配設されて上記空間部1Aを覆う透明かつ酸素透過性を有する膜材3とが液密的に着脱自在に一体化されてなる細胞培養容器を開発するとともに、これを特許文献1において開示している。   Therefore, in order to solve the above-mentioned problems, the present inventors previously formed a plate-like main body in which a space 1A that penetrates between both surfaces and is filled with a culture solution is formed as shown in FIG. 1, a culture plate 2 that is disposed on one surface of the main body 1 to block the space portion 1A and has a cell adhesion property on the surface of the space portion 1A, and the other surface of the main body 1 In addition to developing a cell culture vessel in which the transparent and oxygen-permeable membrane material 3 covering the space 1A is liquid-tightly and detachably integrated, this is disclosed in Patent Document 1. .

上記構成からなる細胞培養容器によれば、膜材3を通じて空間部1A内に常時一様の酸素が供給されるために、酸素供給用の設備が不要となり、付帯設備の簡易化を図ることができる。
特開2002−153261号公報
According to the cell culture container having the above-described configuration, since uniform oxygen is always supplied into the space 1A through the membrane material 3, no oxygen supply facility is required, and the incidental facilities can be simplified. it can.
JP 2002-153261 A

しかしながら、上記従来の細胞培養容器においては、周囲の相対湿度が低い場合に、培養液中に気泡が発生するという現象が起こり、その気泡が細胞の観察を妨げるだけでなく、気泡周囲の培養環境の均一性を損ない、細胞培養の障害になるという問題点があった。そのため、上記従来の細胞培養容器においては、高相対湿度の環境のみでしか使用することができず、低相対湿度の環境下で使用する際には、保湿用の設備が別途必要になるという問題点があった。
また、培養容器に対して加速度が加わった場合あるいは意図的に加速度を負荷しようとする場合に、気泡と培養液の密度差によって培養液が不規則に流動し、培養条件の均一性が損なわれるという問題点もあった。
However, in the above conventional cell culture container, when the surrounding relative humidity is low, a phenomenon occurs in which bubbles are generated in the culture solution, which not only hinders the observation of cells but also the culture environment around the bubbles. There is a problem that the uniformity of the cell is impaired and the cell culture becomes an obstacle. Therefore, the conventional cell culture vessel can be used only in an environment with a high relative humidity, and when used in an environment with a low relative humidity, a separate facility for moisturizing is required. There was a point.
In addition, when acceleration is applied to the culture vessel or when the acceleration is intentionally applied, the culture fluid flows irregularly due to the density difference between the bubbles and the culture fluid, and the uniformity of the culture conditions is impaired. There was also a problem.

本発明は、かかる事情に鑑みてなされたもので、ガス透過性の膜材を利用して培養液に酸素供給を行う場合においても、周囲の相対湿度に関わりなく、培養過程で培養液中に気泡が発生するのを防止することができ、これによって、付帯設備の簡易化を図ることができる細胞培養容器を提供することを目的とする。   The present invention has been made in view of such circumstances, and even when oxygen is supplied to a culture solution using a gas-permeable membrane material, the culture solution can be used in the culture process regardless of the relative humidity of the surroundings. It is an object of the present invention to provide a cell culture container that can prevent the generation of bubbles and thereby simplify the incidental equipment.

本発明者等は、培養液中に気泡が発生するメカニズムについて鋭意研究を重ねた結果、次のような知見を得るに至った。すなわち、空気中の水蒸気が飽和状態でないときには、空気中の水蒸気の分圧が気泡中の水蒸気の分圧よりも低くなる分、その他のガス成分(酸素、窒素など)の分圧が気泡中よりも空気中の方が高くなるために、上記その他のガス成分が膜材を通じて気泡に輸送されて、気泡が徐々に大きくなるという現象が発生する。例えば37℃における飽和水蒸気圧はTetens(1930)の式から求められ6.276kPaとなる。つまり相対湿度100%と50%での圧力差0.03気圧が輸送の原動力となる。これに対して、空気中の水蒸気が飽和状態にあるときには、各ガス成分の分圧が空気中と気泡中とでほぼ等しくなるために、上述したような気泡へのガスの輸送が発生せず、よって気泡が成長するという現象も起こらないと考えられる。   As a result of intensive studies on the mechanism by which bubbles are generated in the culture solution, the present inventors have obtained the following knowledge. That is, when the water vapor in the air is not saturated, the partial pressure of the water vapor in the air is lower than the partial pressure of the water vapor in the bubble, and the partial pressure of other gas components (oxygen, nitrogen, etc.) However, since the air is higher, the other gas components are transported to the bubbles through the membrane material, and the phenomenon that the bubbles gradually increase occurs. For example, the saturated water vapor pressure at 37 ° C. is obtained from the equation of Tetens (1930) and is 6.276 kPa. That is, the pressure difference of 0.03 atm between the relative humidity of 100% and 50% is the driving force for transportation. In contrast, when the water vapor in the air is in a saturated state, the partial pressure of each gas component is almost equal in the air and in the bubbles, so that the gas transport to the bubbles as described above does not occur. Therefore, it is thought that the phenomenon of bubbles growing does not occur.

本発明者等は、このような気泡発生メカニズムに着目して、更なる研究を進めた結果、上記膜材の外面側に水溶液の層を形成して、培養液のガス交換を水溶液中の溶存ガスとの間で行うようにすれば、培養液中に気泡が発生するのを効果的に防止できることを見出し、本発明を完成させたものである。   As a result of further research focusing on such a bubble generation mechanism, the present inventors formed an aqueous solution layer on the outer surface side of the membrane material, and the gas exchange of the culture solution was dissolved in the aqueous solution. It has been found that if it is carried out between gases, bubbles can be effectively prevented from being generated in the culture solution, and the present invention has been completed.

すなわち、請求項1に記載の本発明に係る細胞培養容器は、両面間に貫通し、内部に培養液が充填されて細胞培養が行われる培養空間とされる孔部が形成された第1板状部材と、両面間に貫通し、内部に水または水溶液が充填されて水溶液充填空間とされる孔部が形成された第2板状部材とを有し、上記第1板状部材の外面側に、上記培養空間を塞ぐとともに内面が細胞付着性を有する培養板が配設され、上記第1および第2板状部材の対向面間に、上記培養空間と上記水溶液充填空間とを隔てるとともにガス透過性を有する第1膜材が介装され、かつ上記第2板状部材の外面側に、上記水溶液充填空間を密閉するとともにガス透過性を有する第2膜材が配設されていることを特徴とするものである。なお、上記水には純水も含まれる。 That is, the cell culture vessel according to the present invention as set forth in claim 1, the first plate penetrate between both surfaces, hole portions inside the culture solution are filled in the culture space in which the cell culture is carried out is formed And a second plate-like member penetrating between both surfaces and filled with water or an aqueous solution to form a space filled with an aqueous solution , the outer surface side of the first plate-like member In addition, a culture plate that closes the culture space and has an inner cell adhesion property is disposed, and the culture space and the aqueous solution-filled space are separated between the opposing surfaces of the first and second plate-like members and gas A first membrane material having permeability is interposed, and a second membrane material having gas permeability is disposed on the outer surface side of the second plate member while sealing the aqueous solution filling space. It is a feature. The water includes pure water.

請求項1に記載の発明によれば、第2膜材を介して外部の空気と水溶液中の溶存ガスとの間でガス交換が行われ、その際に、空気中の水蒸気分圧が低いと、その分他のガス分圧が上がって飽和を超えることとなり、水溶液中に気泡が発生することとなるが、培養液のガス交換が第1膜材を介して水溶液中の溶存ガスとの間で行われ、この水溶液中のガス分圧が平衡となるために、培養液においては気泡が発生しなくなる。   According to the first aspect of the present invention, gas exchange is performed between the external air and the dissolved gas in the aqueous solution via the second membrane material, and at that time, if the water vapor partial pressure in the air is low Therefore, the gas partial pressure increases and exceeds saturation, and bubbles are generated in the aqueous solution. However, gas exchange of the culture solution is performed between the dissolved gas in the aqueous solution via the first membrane material. Since the gas partial pressure in this aqueous solution is in equilibrium, no bubbles are generated in the culture solution.

請求項2に記載の発明は、請求項1に記載の細胞培養容器において、上記水溶液として、上記培養液またはそのベースとなる基礎培養液を用いたことを特徴とするものである。 The invention described in claim 2 is characterized in that, in the cell culture container according to claim 1, the culture solution or a basic culture solution serving as a base thereof is used as the aqueous solution.

本発明によれば、ガス透過性の膜材を利用して培養液に酸素供給を行う場合においても、周囲の相対湿度に関わりなく、培養過程で培養液中に気泡が発生するのを防止することができる。したがって、気泡の発生を防止するための保湿用の設備を別途設ける必要がなくなり、付帯設備の簡易化を図ることができる。また、培養液に気泡が発生しなくなることから、培養環境の均一性や観察性の向上を図ることができ、気泡発生に起因する種々の問題点を解消することができる。   According to the present invention, even when oxygen is supplied to a culture solution using a gas permeable membrane material, bubbles are prevented from being generated in the culture solution during the culture process, regardless of the relative humidity of the surroundings. be able to. Accordingly, it is not necessary to separately provide a moisturizing facility for preventing the generation of bubbles, and the incidental facility can be simplified. In addition, since no bubbles are generated in the culture solution, the uniformity of the culture environment and the observability can be improved, and various problems caused by the generation of bubbles can be solved.

図1および図2は、本発明に係る細胞培養容器の一実施形態を示すもので、図中符号10が、フッ素樹脂やポリカーボネート、アセタール等の所定の強度と耐食性を有する合成樹脂によって矩形板状に形成された第1板状部材である。この第1板状部材10の中央部には、両面間に貫通する孔部11が形成されており、この孔部11に、培養液を充填して細胞培養を行うための培養空間12が形成されるようになっている。ここで、孔部11は、その稜線が、長手方向の中央部において互いに平行になるとともに、両端部においてV字状に傾斜する6角形状に形成されている。また、第1板状部材10には、一端が培養空間12の長手方向一端に開口し、他端が第1板状部材10の側面に開口する培養液供給孔(図示省略)と、一端が培養空間12の長手方向他端に開口し、第1板状部材10の側部に沿って延びて同様に第1板状部材10の側面に開口する培養液排出孔(図示省略)とが穿設されている。   1 and 2 show an embodiment of a cell culture container according to the present invention. In the figure, reference numeral 10 denotes a rectangular plate shape made of a synthetic resin having a predetermined strength and corrosion resistance, such as fluororesin, polycarbonate, and acetal. It is the 1st plate-shaped member formed in. A hole 11 penetrating between both surfaces is formed at the center of the first plate member 10, and a culture space 12 for filling the culture medium and performing cell culture is formed in the hole 11. It has come to be. Here, the hole part 11 is formed in a hexagonal shape whose ridge lines are parallel to each other in the center part in the longitudinal direction and are inclined in a V shape at both end parts. The first plate-like member 10 has one end opened at one end in the longitudinal direction of the culture space 12 and the other end opened at the side of the first plate-like member 10 and one end thereof. A culture medium discharge hole (not shown) that opens to the other longitudinal end of the culture space 12, extends along the side of the first plate member 10, and similarly opens to the side surface of the first plate member 10. It is installed.

この第1板状部材10の一方の面側(外面側)には、表面が細胞付着性を有するポリスチレン等の素材によって矩形状に形成された培養板30が設けられ、他方の面側(内面側)には、例えばフッ素樹脂、シリコーン、ポリメチルペンテン等からなる透明でかつガス透過性を有する薄肉素材によって矩形状に形成された第1膜材31が設けられている。これら培養板30および第1膜材31は、第1板状部材10の外面全体および内面全体を覆うように、何れも外形が第1板状部材10とほぼ同寸法に設定されている。すなわち、第1板状部材10の孔部11の両開口が培養板30と第1膜材31とによって塞がれることにより、密閉状態の培養空間12が形成されるようになっている。なお、本実施形態では、第1板状部材10の厚さ寸法が約3mm、培養板30の厚さ寸法が約1.5mm、各膜材31、32の厚さ寸法が約0.1mm、後述する第2板状部材20の厚さ寸法が約2mmにそれぞれ設定されている。   On one surface side (outer surface side) of the first plate-like member 10, a culture plate 30 whose surface is formed in a rectangular shape by a material such as polystyrene having cell adhesion is provided, and the other surface side (inner surface side). The first film material 31 formed in a rectangular shape by a transparent and gas-permeable thin material made of, for example, fluororesin, silicone, polymethylpentene, or the like is provided on the side. The culture plate 30 and the first membrane material 31 are both set to have substantially the same outer dimensions as the first plate member 10 so as to cover the entire outer surface and the entire inner surface of the first plate member 10. That is, when both openings of the hole 11 of the first plate-like member 10 are closed by the culture plate 30 and the first membrane material 31, a sealed culture space 12 is formed. In this embodiment, the thickness dimension of the first plate member 10 is about 3 mm, the thickness dimension of the culture plate 30 is about 1.5 mm, and the thickness dimension of each membrane material 31 and 32 is about 0.1 mm. The thickness dimension of the 2nd plate-shaped member 20 mentioned later is each set to about 2 mm.

第2板状部材20は、第1板状部材10と同質の素材により同平面形状に形成された板状部材であって、第1板状部材10との間に第1膜材31を狭持するようになっている。この第2板状部材20の中央部には、第1板状部材10と同様に、両面間に貫通する孔部21が形成されており、この孔部21に、水または水溶液が充填される水溶液充填空間22が形成されるようになっている。この水溶液充填空間22に充填される水溶液としては、種々の水溶液を使用することが可能であるが、水溶液充填空間22と培養空間12との浸透圧の差をなくして培養空間12内の培養液の希釈を抑制するためには、培養空間12と同じ培養液や、そのベースとなる基礎培養液などを水溶液として用いることが好ましい。   The second plate-like member 20 is a plate-like member formed in the same planar shape from the same material as the first plate-like member 10, and the first film material 31 is narrowed between the second plate-like member 20 and the first plate-like member 10. It comes to have. In the center of the second plate-like member 20, a hole 21 penetrating between both surfaces is formed as in the first plate-like member 10, and this hole 21 is filled with water or an aqueous solution. An aqueous solution filling space 22 is formed. Various aqueous solutions can be used as the aqueous solution filled in the aqueous solution filling space 22, but the osmotic pressure difference between the aqueous solution filling space 22 and the culture space 12 is eliminated, and the culture solution in the culture space 12 In order to suppress the dilution, it is preferable to use the same culture solution as the culture space 12 or a basic culture solution as a base thereof as an aqueous solution.

また、第2板状部材20の外面側には、透明でガス透過性を有する第1膜材31と同様の薄肉素材によって矩形状に形成された第2膜材32が設けられている。この第2膜材32は、第2板状部材20の外面全体を覆うように、外形が第2板状部材20とほぼ同寸法に設定されている。すなわち、第2板状部材20の孔部21の両開口が第1膜材31および第2膜材32によって塞がれることにより、密閉状態の水溶液充填空間22が形成されるようになっている。   Further, on the outer surface side of the second plate-like member 20, a second film material 32 formed in a rectangular shape by a thin material similar to the transparent and gas permeable first film material 31 is provided. The outer shape of the second film member 32 is set to be substantially the same as that of the second plate member 20 so as to cover the entire outer surface of the second plate member 20. That is, when both openings of the hole portion 21 of the second plate-like member 20 are closed by the first film material 31 and the second film material 32, a sealed aqueous solution filling space 22 is formed. .

このように本実施形態では、培養板30、第1板状部材10、第1膜材31、第2板状部材20および第2膜材32を順番に積層した状態でそれぞれを一体化することにより、培養空間12および水溶液充填空間22を有する細胞培養容器が構成されている。   Thus, in this embodiment, each is integrated in the state which laminated | stacked the culture plate 30, the 1st plate-shaped member 10, the 1st film | membrane material 31, the 2nd plate-shaped member 20, and the 2nd film | membrane material 32 in order. Thus, a cell culture container having the culture space 12 and the aqueous solution filling space 22 is configured.

上記構成からなる細胞培養容器においては、培養板30に細胞を付着させて、培養空間12に培養液を、水溶液充填空間22に水溶液をそれぞれ充填した状態で、細胞培養が行われる。培養に伴い細胞は呼吸するが、その際に酸素を消費し、炭酸ガスを発生する。その結果、培養液中の溶存酸素は減少して、水溶液中の溶存酸素との間で濃度差が生じることにより、水溶液から溶存酸素が第1膜材31を通じて培養液中に移動する受動輸送が発生する。同様に、水溶液中の溶存酸素濃度が減少すると、空気中の酸素分圧との平衡が崩れて、酸素が水溶液中に移動する受動輸送が発生する。一方、炭酸ガスについても、培養液中の溶存濃度が増大することにより、培養液中の溶存ガスが水溶液に移動して当該水溶液中の溶存ガスが空気中に放出される受動輸送が発生する。このように各ガス成分について受動輸送が発生することにより、培養液中の各ガス成分の濃度がほぼ一定に保持されることとなる。   In the cell culture container having the above-described configuration, cell culture is performed in a state where cells are attached to the culture plate 30 and the culture space 12 is filled with the culture solution and the aqueous solution filling space 22 is filled with the aqueous solution. The cells breathe as they are cultured, but at that time they consume oxygen and generate carbon dioxide. As a result, the dissolved oxygen in the culture solution decreases and a difference in concentration occurs with the dissolved oxygen in the aqueous solution, so that passive transport in which the dissolved oxygen moves from the aqueous solution through the first membrane material 31 into the culture solution is performed. appear. Similarly, when the dissolved oxygen concentration in the aqueous solution decreases, the equilibrium with the oxygen partial pressure in the air is lost, and passive transport in which oxygen moves into the aqueous solution occurs. On the other hand, as for the carbon dioxide gas, when the dissolved concentration in the culture solution increases, passive transport occurs in which the dissolved gas in the culture solution moves to the aqueous solution and the dissolved gas in the aqueous solution is released into the air. As described above, when the passive transport occurs for each gas component, the concentration of each gas component in the culture solution is maintained almost constant.

また、空気中の水蒸気が飽和状態でないときには、その分他のガス成分(酸素、窒素など)の分圧が高くなる。このとき、水溶液中に発生した気泡中の上記他のガス成分の分圧は、同じ大気圧の場合、水蒸気の分圧が高い分低くなっている。そのため水溶液中の気泡に上記他のガスが輸送されて大きくなる。しかし水溶液中のガス分圧は平衡となるため、培養液に気泡が発生することがない。   Further, when the water vapor in the air is not saturated, the partial pressure of other gas components (oxygen, nitrogen, etc.) increases accordingly. At this time, the partial pressures of the other gas components in the bubbles generated in the aqueous solution are low because the partial pressure of water vapor is high when the atmospheric pressure is the same. Therefore, the other gas is transported to the bubbles in the aqueous solution and becomes larger. However, since the gas partial pressure in the aqueous solution is balanced, no bubbles are generated in the culture solution.

以上のように、本実施形態の細胞培養容器によれば、培養液を覆う第1膜材31の外面側に水溶液の層が形成されて、培養液のガス交換が水溶液中の溶存ガスとの間で行われることとなるので、周囲の相対湿度に関わりなく、培養過程で培養液中に気泡が発生するのを防止することができる。したがって、気泡の発生を防止するための保湿用の設備を別途設ける必要がなくなり、付帯設備の簡易化を図ることができる。また、培養液に気泡が発生しなくなることから、培養環境の均一性や観察性の向上を図ることができ、気泡発生に起因する種々の問題点を解消することができる。   As described above, according to the cell culture container of the present embodiment, the aqueous solution layer is formed on the outer surface side of the first membrane material 31 covering the culture solution, and the gas exchange of the culture solution is performed with the dissolved gas in the aqueous solution. Therefore, it is possible to prevent bubbles from being generated in the culture medium during the culture process regardless of the relative humidity of the surroundings. Accordingly, it is not necessary to separately provide a moisturizing facility for preventing the generation of bubbles, and the incidental facility can be simplified. In addition, since no bubbles are generated in the culture solution, the uniformity of the culture environment and the observability can be improved, and various problems caused by the generation of bubbles can be solved.

次に、本発明の効果を実施例により明らかにする。
本発明を適用した実施例では、3cm×6cmの袋状に形成した厚さ0.2mmのシリコーンフィルムバッグの中に水を入れ、空気が入らないように封をした。そして、水を張った培養皿に、作製したシリコーンフィルムバッグを沈めて、22℃、相対湿度60%の設定条件下でインキュベータにより110時間保温し、その前後の質量を比較するとともに気泡の発生状況を観察した。なお、この実施例では、シリコーンフィルムバッグが本発明に係る細胞培養容器の第1膜材に対応し、シリコーンフィルムバッグの内部が培養空間に対応し、培養皿の内面とシリコーンフィルムバッグの外面との間に形成される空間が水溶液充填空間に対応するものである。
Next, the effect of the present invention will be clarified by examples.
In the example to which the present invention was applied, water was put into a 0.2 mm thick silicone film bag formed in a 3 cm × 6 cm bag shape and sealed so as not to enter air. Then, the produced silicone film bag is submerged in a culture dish filled with water, and kept in an incubator for 110 hours under the setting conditions of 22 ° C. and a relative humidity of 60%. Was observed. In this embodiment, the silicone film bag corresponds to the first membrane material of the cell culture container according to the present invention, the interior of the silicone film bag corresponds to the culture space, the inner surface of the culture dish, the outer surface of the silicone film bag, The space formed between the two corresponds to the aqueous solution filling space.

これに対して、比較例1では、実施例と同様に作製したシリコーンフィルムバッグを、水を張らない培養皿に置くようにして、これ以外の条件を実施例と同条件とした。この比較例1は、空気中の水蒸気が飽和状態でないときに、従来の細胞培養容器(培養液を覆う膜材3の外面側に水溶液の層が形成されていない細胞培養容器)を使用した場合に対応するものである。一方、比較例2では、比較例1と同様に、水を張らない培養皿にシリコーンフィルムバッグを置いて、これを24℃、相対湿度100%の設定条件下でインキュベータにより110時間保温するようにした。この比較例2は、空気中の水蒸気が飽和状態にあるときに、従来の細胞培養容器を使用した場合に対応するものである。実施例および各比較例のシリコーンフィルムバッグの試験前後の変化を表1に示す。   On the other hand, in Comparative Example 1, the silicone film bag produced in the same manner as in the example was placed on a culture dish not filled with water, and the other conditions were the same as those in the example. In Comparative Example 1, when water vapor in the air is not saturated, a conventional cell culture vessel (a cell culture vessel in which an aqueous solution layer is not formed on the outer surface side of the membrane material 3 covering the culture solution) is used. It corresponds to. On the other hand, in Comparative Example 2, as in Comparative Example 1, a silicone film bag was placed on a culture dish that was not filled with water, and this was kept warm for 110 hours in an incubator under the setting conditions of 24 ° C. and relative humidity of 100%. did. This comparative example 2 corresponds to the case where a conventional cell culture vessel is used when water vapor in the air is saturated. Table 1 shows the changes before and after the test of the silicone film bags of Examples and Comparative Examples.

Figure 0004378514
Figure 0004378514

この表1からわかるように、実施例では、シリコーンフィルムバッグ内に気泡が発生せず、試験前後でシリコーンフィルムバッグの質量に僅かな変化(約2%の減少)しか見られなかったのに対して、比較例1では、シリコーンフィルムバッグ内に約2mlの気泡が発生し、シリコーンフィルムバッグの質量についても実施例よりも大きな変化(約10%の減少)が見られた。他方、比較例2では、実施例と同様に、シリコーンフィルムバッグ内に気泡が発生せず、試験前後でシリコーンフィルムバッグの質量に殆ど変化がなかった。
このように、従来の細胞培養容器に対応する比較例では、周囲の相対湿度如何によって、気泡の発生状況が大きく変化するのに対して、本発明を適用した実施例においては、周囲の相対湿度に関わりなく、気泡の発生を防止できることが確認された。
As can be seen from Table 1, in the examples, no bubbles were generated in the silicone film bag, and only a slight change (a decrease of about 2%) was observed in the mass of the silicone film bag before and after the test. In Comparative Example 1, about 2 ml of bubbles were generated in the silicone film bag, and the change of the mass of the silicone film bag was also larger (about 10% decrease) than the Example. On the other hand, in Comparative Example 2, as in the example, no bubbles were generated in the silicone film bag, and there was almost no change in the mass of the silicone film bag before and after the test.
As described above, in the comparative example corresponding to the conventional cell culture vessel, the generation state of bubbles greatly changes depending on the relative humidity of the surroundings, whereas in the example to which the present invention is applied, the relative humidity of the surroundings Regardless, it was confirmed that the generation of bubbles can be prevented.

本発明に係る細胞培養容器の一実施形態を示す分解斜視図である。It is a disassembled perspective view which shows one Embodiment of the cell culture container which concerns on this invention. 図1の細胞培養容器の断面図である。It is sectional drawing of the cell culture container of FIG. 従来の細胞培養容器の一例を示す分解斜視図である。It is a disassembled perspective view which shows an example of the conventional cell culture container.

符号の説明Explanation of symbols

10 第1板状部材
12 培養空間
20 第2板状部材
22 水溶液充填空間
30 培養板
31 第1膜材
32 第2膜材
DESCRIPTION OF SYMBOLS 10 1st plate-shaped member 12 Culture space 20 2nd plate-shaped member 22 Aqueous solution filling space 30 Culture plate 31 1st film material 32 2nd film material

Claims (2)

両面間に貫通し、内部に培養液が充填されて細胞培養が行われる培養空間とされる孔部が形成された第1板状部材と、両面間に貫通し、内部に水または水溶液が充填されて水溶液充填空間とされる孔部が形成された第2板状部材とを有し、
上記第1板状部材の外面側に、上記培養空間を塞ぐとともに内面が細胞付着性を有する培養板が配設され、
上記第1および第2板状部材の対向面間に、上記培養空間と上記水溶液充填空間とを隔てるとともにガス透過性を有する第1膜材が介装され、
かつ上記第2板状部材の外面側に、上記水溶液充填空間を密閉するとともにガス透過性を有する第2膜材が配設されていることを特徴とする細胞培養容器。
A first plate-like member that has a hole that is a culture space in which cell culture is performed by filling the inside with a culture solution , and between both sides, and is filled with water or an aqueous solution inside And a second plate-like member having a hole formed as an aqueous solution filling space ,
A culture plate that closes the culture space and has cell adhesion on the outer surface side of the first plate member is disposed,
Between the opposing surfaces of the first and second plate-like members, a first membrane material having a gas permeability is provided between the culture space and the aqueous solution filling space ,
And above the outer surface of the second plate member, the cell culture vessel, wherein the second film material having a gas permeability as well as sealing the solution filling space is provided.
上記水溶液として、上記培養液またはそのベースとなる基礎培養液を用いたことを特徴とする請求項1に記載の細胞培養容器。 2. The cell culture vessel according to claim 1, wherein the aqueous solution is the culture solution or a basic culture solution serving as a base thereof .
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