JP4445765B2 - Cell culture equipment - Google Patents
Cell culture equipment Download PDFInfo
- Publication number
- JP4445765B2 JP4445765B2 JP2004029795A JP2004029795A JP4445765B2 JP 4445765 B2 JP4445765 B2 JP 4445765B2 JP 2004029795 A JP2004029795 A JP 2004029795A JP 2004029795 A JP2004029795 A JP 2004029795A JP 4445765 B2 JP4445765 B2 JP 4445765B2
- Authority
- JP
- Japan
- Prior art keywords
- culture
- cells
- culture solution
- dimensional
- cell culture
- 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.)
- Expired - Fee Related
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M25/00—Means for supporting, enclosing or fixing the microorganisms, e.g. immunocoatings
- C12M25/14—Scaffolds; Matrices
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/20—Degassing; Venting; Bubble traps
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/26—Means for regulation, monitoring, measurement or control, e.g. flow regulation of pH
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/30—Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration
- C12M41/34—Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration of gas
Description
本発明は、種々の形状や大きさの三次元基材上に播種された細胞を、高い効率で、しかも高密度に培養することができる細胞培養装置に関する。 The present invention relates to a cell culture apparatus capable of culturing cells seeded on a three-dimensional substrate of various shapes and sizes with high efficiency and high density.
近年の細胞工学技術の進展によって、ヒト細胞を含む数々の動物細胞の培養が可能となり、また、それらの細胞を用いてヒトの組織や器官を再構築しようとする、いわゆる再生医療の研究が急速に進んでいる。再生医療においては、細胞が増殖分化して三次元的な生体組織様の構造物を構築できるかがポイントである。通常、このような生体組織様構造体を製造する場合、組織又は器官の再生の足場になる三次元基材上に細胞を播種し、培養することが行われる。このようにして得られた生体組織様構造体を患者に移植すれば、生体組織様構造体が組織又は器官と同様の機能を発揮したり、生体組織様構造体を足場にして患者自身の組織又は器官が再生したりする。
一般に、ヒトの組織又は器官は、種々の細胞が細胞間物質を介して極めて高密度に集積した構造を有しており、再生医療に用いる生体組織様構造体でも、このような組織又は器官にできる限り近い構造が形成されていることが重要である。
Recent advances in cell engineering technology have enabled the culturing of numerous animal cells, including human cells, and rapid research on so-called regenerative medicine that uses these cells to reconstruct human tissues and organs. Is going on. In regenerative medicine, the point is whether cells can proliferate and differentiate to construct a three-dimensional biological tissue-like structure. Usually, when such a biological tissue-like structure is produced, cells are seeded and cultured on a three-dimensional substrate that serves as a scaffold for tissue or organ regeneration. If the biological tissue-like structure obtained in this way is transplanted into a patient, the biological tissue-like structure performs the same function as the tissue or organ, or the patient's own tissue using the biological tissue-like structure as a scaffold Or an organ regenerates.
In general, a human tissue or organ has a structure in which various cells are accumulated at a very high density via an intercellular substance, and a biological tissue-like structure used for regenerative medicine is also included in such a tissue or organ. It is important that a structure as close as possible is formed.
一方、再生医療分野に限らず、例えば、化粧品や医薬品の研究等の用途にも大量の動物細胞が必要とされており、このような大量の細胞を得る手段として、三次元基材上に播種した細胞を高密度に培養した後、該三次元基材から細胞を剥離して回収することが試みられている。 On the other hand, not only in the field of regenerative medicine, for example, a large amount of animal cells are also required for research such as cosmetics and pharmaceuticals. As a means for obtaining such a large amount of cells, seeding on a three-dimensional substrate is performed. Attempts have been made to detach and collect cells from the three-dimensional substrate after culturing such cells at high density.
これらのいずれの用途においても、三次元基材に播種された細胞を高密度に培養する方法が求められている。
従来の細胞培養法としては、例えば、細胞培養用フラスコの底面に細胞を接着させ、この細胞培養用フラスコに所定量の培養液を添加し、CO2インキュベータ等内で静置して培養する静置培養法が挙げられる。しかし、静置培養法は、細胞培養用フラスコの底面を覆い尽くす程度までの細胞数を培養する場合しか想定していないものであった。細胞密度が極めて高く、大量の細胞を含有する生体組織様構造体を従来の静置培養法により培養すると、ごく短時間の間に培養液中に含まれる栄養成分が不足したり、細胞の分泌する老廃物によって培養液のpHが変動してしまい、細胞増殖速度が著しく制限されたり、場合によっては細胞が死滅してしまうことがあった。
これに対して、大量の培養液を用いたり、培養液の交換サイクルを短くしたりする等が考えられるが、このような方法によれば、大型の装置を要したり、微生物による汚染の生じる確率が格段に高くなる等の問題点があった。
In any of these uses, a method for culturing cells seeded on a three-dimensional substrate at high density is required.
As a conventional cell culture method, for example, a cell is adhered to the bottom of a cell culture flask, a predetermined amount of a culture solution is added to the cell culture flask, and the cell culture flask is left to stand in a CO 2 incubator or the like. Incubation method is mentioned. However, the stationary culture method is supposed only to cultivate the number of cells up to the extent that the bottom of the cell culture flask is covered. When living tissue-like structures with extremely high cell density and containing a large number of cells are cultured by the conventional static culture method, nutrient components contained in the culture are insufficient or the cells are secreted in a very short time. The pH of the culture solution fluctuates due to the waste product, and the cell growth rate is remarkably restricted, or the cells may be killed in some cases.
On the other hand, it is conceivable to use a large amount of culture solution or shorten the exchange cycle of the culture solution. However, according to such a method, a large apparatus is required or contamination with microorganisms occurs. There was a problem that the probability became much higher.
また、三次元基材に播種された細胞は、最も環境の良い基材表面に付着し増殖した後に、コラーゲン等の細胞外マトリックスを分泌して三次元基材の表面を覆ってしまうことが多い。このように細胞外マトリックスにより覆われた三次元基材においては、培養液が三次元基材の内部にまでは供給されにくくなることから、細胞は基材の表面のみに留まって基材の内部にまでは侵入しなかったり、播種の段階では三次元基材の内部にまで均一に侵入していた細胞も培地からの栄養や酸素を受け取ることができず充分に増殖できなかったりして、期待したほどの高密度培養はできないという問題があった。 In addition, cells seeded on a three-dimensional substrate often adhere to the surface of the substrate with the best environment and proliferate, and then secrete an extracellular matrix such as collagen to cover the surface of the three-dimensional substrate. . In the three-dimensional base material covered with the extracellular matrix in this manner, the culture solution is difficult to be supplied to the inside of the three-dimensional base material, so that the cells remain only on the surface of the base material and remain inside the base material. The cells that had penetrated uniformly to the inside of the three-dimensional substrate at the seeding stage could not receive nutrients and oxygen from the medium and could not grow sufficiently, so expected. There was a problem that high-density culture was not possible.
更に、とりわけ再生医療に用いるための生体組織様構造体を製造する場合には、移植の部位や目的によって種々の形状や大きさの三次元基材上で細胞を培養する必要があるところ、従来は画一的な形状、大きさのものを培養できる細胞培養装置しかないのが現状であった。従って、形状や大きさが異なる三次元基材上で細胞を培養をする場合には、各三次元基材ごとに細胞培養装置を新たに製造する必要があり、極めてコストパフォーマンスが悪い状況にあった。 Furthermore, when manufacturing a biological tissue-like structure for use in regenerative medicine in particular, it is necessary to culture cells on a three-dimensional substrate of various shapes and sizes depending on the site and purpose of transplantation. At present, there is only a cell culture device capable of culturing uniform shapes and sizes. Therefore, when cells are cultured on three-dimensional substrates having different shapes and sizes, it is necessary to newly manufacture a cell culture device for each three-dimensional substrate, and the cost performance is extremely poor. It was.
本発明は、上記現状に鑑み、種々の形状や大きさの三次元基材上に播種された細胞を、高い効率で、しかも高密度に培養することができる細胞培養装置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 apparatus capable of culturing cells seeded on a three-dimensional base material of various shapes and sizes with high efficiency and high density in view of the above-mentioned present situation. And
本発明は、系内を循環する培養液を用いて三次元基材上に播種した細胞を培養する細胞培養装置であって、細胞が接着した三次元基材を担持する手段、培養液を循環させる手段、培養液中の気泡を脱泡する手段、並びに、培養液のpH、溶存酸素濃度及び温度を調製する手段を有し、前記細胞が接着した三次元基材を担持する手段がユニット化されており、複数のユニットを着脱可能とした細胞培養装置である。
以下に本発明を詳述する。
The present invention relates to a cell culture apparatus for culturing cells seeded on a three-dimensional substrate using a culture medium circulating in the system, means for supporting the three-dimensional substrate to which the cells are adhered, and circulating the culture liquid A means for defoaming bubbles in the culture solution, a means for adjusting the pH, dissolved oxygen concentration and temperature of the culture solution, and means for supporting the three-dimensional substrate to which the cells are attached A cell culture device in which a plurality of units can be attached and detached.
The present invention is described in detail below.
本発明の細胞培養装置は、少なくとも、細胞が接着した三次元基材を担持する手段(以下、基材担持手段ともいう)、培養液を循環させる手段(以下、循環手段ともいう)、培養液中の気泡を脱泡する手段(以下、脱泡手段ともいう)、及び、培養液のpH、溶存酸素濃度、温度を調製する手段(以下、培養液調整手段ともいう)を有する。 The cell culture apparatus of the present invention comprises at least means for supporting a three-dimensional substrate to which cells are adhered (hereinafter also referred to as substrate supporting means), means for circulating a culture solution (hereinafter also referred to as circulation means), culture solution Means for defoaming the bubbles therein (hereinafter also referred to as defoaming means) and means for adjusting the pH, dissolved oxygen concentration and temperature of the culture solution (hereinafter also referred to as culture solution adjusting means).
上記基材担持手段は、三次元基材が型崩れしないように保持できるものであれば特に限定されないが、目的とする細胞が播種された三次元基材と形状及び大きさが略同じである空隙部と、前記空隙部を挟んだ両端に培養液流入口と培養液流出部とが配置された構造を有するものが好ましい。基材保持手段の空隙部と三次元基材との形状及び大きさが同じでないと、培養液が選択的に基材保持手段と三次元基材との間にできた隙間を流れてしまうため、三次元基材内に充分に培養液が循環しなくなってしまうことがある。
このような基材担持手段の1態様の断面を示す模式図を図1に示した。
The substrate supporting means is not particularly limited as long as the three-dimensional substrate can be held so as not to lose its shape, but is substantially the same in shape and size as the three-dimensional substrate seeded with the target cells. What has the structure where the culture solution inflow port and the culture solution outflow part are arrange | positioned at the both ends which pinched | interposed the space | gap part with the space | gap part is preferable. If the shape and size of the gap between the substrate holding means and the three-dimensional substrate are not the same, the culture solution will selectively flow through the gap formed between the substrate holding means and the three-dimensional substrate. The culture solution may not circulate sufficiently in the three-dimensional substrate.
A schematic diagram showing a cross section of one embodiment of such a substrate supporting means is shown in FIG.
図1に示した基材担持手段1は、三次元基材を配置するための空隙部2を有し、この空隙部2の両側にそれぞれ培養液流入口3と培養液流出口4とが配置されたホルダー状のものである。図1に示した基材担持手段は、ネジ構造等により嵌合する構造となっており、これを開閉することにより細胞を播種した三次元基材を空隙部2中に配置することができる。また、空隙部2においては、配置した三次元基材が型崩れしないようにスペーサ10を介して2枚のサポートフィルタ11に三次元基材を挟み込めるようにしておいてもよい。
図1に示した基材担持手段1において、空隙部2の形状及び大きさを目的とする三次元基材と同一とすれば、培養液流入口3から流入した培養液は、強制的に三次元基材の内部を通過して培養液流出口4から流出する。従って、三次元基材の内部にまで確実に培養液が循環することから、高い効率で、しかも高密度に細胞を増殖させることができる。
The substrate supporting means 1 shown in FIG. 1 has a
In the base material supporting means 1 shown in FIG. 1, if the shape and size of the
なお、本発明の細胞培養装置において、上記基材担持手段はいずれの向きに配置しても構わないが、上記培養液流入口が下部に、上記培養液流出口が上部になるように配置することが好ましい。このように配置した場合には、より確実に三次元基材の内部に培養液を通過させることができる。 In the cell culture apparatus of the present invention, the substrate supporting means may be arranged in any direction, but is arranged so that the culture solution inlet is at the bottom and the culture solution outlet is at the top. It is preferable. When it arrange | positions in this way, a culture solution can be made to pass through the inside of a three-dimensional base material more reliably.
本発明の細胞培養装置は、上記基材担持手段がユニット化されており、複数のユニットが着脱可能である。これにより、形状や大きさの異なる複数の三次元基材に接着した細胞を、1つの装置で同時に培養することができる。また、特殊な形状の三次元基材上で細胞を培養する場合でも、この基材担持手段のみを作製すれば直ちに本発明の細胞培養装置で培養することができ、極めてコストパフォーマンスに優れる。
上記ユニット化された基材担持手段の1例を示す模式図を図2に示した。
図2に示したユニット5では、基材担持手段1の他、後述する脱泡手段6も含まれる。培養液は脱泡手段6を通して脱泡された後、培養液流入口3を通って基材担持手段1に流入し、空隙部2に設置された細胞が播種された三次元基材中を通過した後、培養液流出口4から流出する。図2に示したユニット5は、スライド式に細胞培養装置に装着できるようになっていることから、装着操作も極めて容易である。
本発明の細胞培養装置は、このようなユニットを複数着脱することができる。
In the cell culture apparatus of the present invention, the substrate supporting means is unitized, and a plurality of units can be attached and detached. Thereby, the cell adhere | attached on the several three-dimensional base material from which a shape and a magnitude | size differ can be culture | cultivated simultaneously with one apparatus. Even when cells are cultured on a specially-shaped three-dimensional substrate, if only the substrate supporting means is produced, it can be immediately cultured with the cell culture apparatus of the present invention, and the cost performance is extremely excellent.
A schematic diagram showing an example of the unitized substrate supporting means is shown in FIG.
The
The cell culture device of the present invention can attach and detach a plurality of such units.
上記循環手段としては、一定量の培養液を正確に循環させることができるものであれば特に限定されないが、低流量の培養液を安定して循環させることができることからチューブポンプが好適である。上記チューブポンプとしては、通常市販されているものを用いることができる。また、脈流等の規則的な変動流で培養液を循環させるために、プログラマブルポンプやダブルプランジャータイプのポンプを用いることもできる。
なお、チューブポンプを用いて培養液を循環させる場合、各々のチューブは上記基材担持手段に1つずつ接続されることが好ましい。これにより、上記基材担持手段に供給される培養液の流量をより正確に制御することができる。
The circulating means is not particularly limited as long as it can circulate a certain amount of culture broth accurately, but a tube pump is suitable because it can circulate a low flow rate culture broth stably. As the tube pump, a commercially available one can be used. In addition, a programmable pump or a double plunger type pump can also be used to circulate the culture solution in a regular fluctuating flow such as a pulsating flow.
In addition, when circulating a culture solution using a tube pump, it is preferable that each tube is connected to the said base material carrying means 1 each. Thereby, the flow volume of the culture solution supplied to the said base material support means can be controlled more correctly.
上記脱泡手段としては特に限定されず、従来公知の方法を用いることができるが、例えば、適当な容量の液溜まり部分に培養液を導き、液溜まりの上部に溜まった気泡を外部に放出させる方法等が簡便で好ましい。 The defoaming means is not particularly limited, and a conventionally known method can be used. For example, the culture solution is introduced into a liquid reservoir portion having an appropriate volume, and bubbles accumulated in the upper portion of the liquid reservoir are released to the outside. The method is simple and preferable.
上記培養液調整手段としては特に限定されないが、例えば、二酸化炭素及び酸素濃度が調整されたガスを供給する手段等が好ましい。通常、培養液は緩衝機能を有する緩衝液とされていることから、細胞の分泌する老廃物によって培養液のpHが変動したり、細胞によって培養液中の酸素が消費されてしまったりした場合でも、二酸化炭素及び酸素濃度が調整されたガスを供給することにより容易にそのpHを生理的なpHに調整し、また、酸素を溶解することができる。特に、二酸化炭素及び酸素濃度が調整されたガスとして加湿されたガスを用いれば、培養液からの水分の蒸発を抑制することができることから好ましい。
また、培養液の温度を調整する手段としては、培養液のみをヒーター等を用いて加温してもよいが、装置自体を極めてコンパクトにできることから、装置全体を市販のインキュベータ中に設置することにより温度調整してもよい。
The culture medium adjusting means is not particularly limited, but for example, means for supplying a gas whose carbon dioxide and oxygen concentrations are adjusted is preferable. Usually, since the culture solution is a buffer solution having a buffer function, even if the pH of the culture solution fluctuates due to waste products secreted by the cells, or oxygen in the culture solution is consumed by the cells The pH can be easily adjusted to a physiological pH by supplying carbon dioxide and a gas whose oxygen concentration is adjusted, and oxygen can be dissolved. In particular, it is preferable to use a humidified gas as the gas whose carbon dioxide and oxygen concentrations are adjusted, because evaporation of moisture from the culture solution can be suppressed.
In addition, as a means of adjusting the temperature of the culture solution, only the culture solution may be heated using a heater or the like. However, since the device itself can be made extremely compact, the entire device should be installed in a commercially available incubator. You may adjust temperature by.
上記培養液調整手段が二酸化炭素及び酸素濃度が調整されたガスを供給する手段である場合、循環している培養液に直接二酸化炭素及び酸素濃度が調整され、加湿されたガスを吹き込んでもよいが、培養液に大量の気泡が発生してしまうことがある。そこで、本発明の細胞培養装置に、培養液貯留槽を設け、この培養液貯留槽の気相中に二酸化炭素及び酸素濃度が調整されたガスを吹き込みようにすれば、培養液の気液界面においてガス交換して、気泡を生じることなく培養液のpHを調整することができることから好ましい。 When the culture medium adjusting means is a means for supplying a gas with adjusted carbon dioxide and oxygen concentration, the carbon dioxide and oxygen concentration may be directly adjusted and the humidified gas may be blown into the circulating culture medium. A large amount of bubbles may be generated in the culture solution. Therefore, if the cell culture apparatus of the present invention is provided with a culture solution storage tank, and a gas with adjusted carbon dioxide and oxygen concentration is blown into the gas phase of the culture solution storage tank, the gas-liquid interface of the culture solution It is preferable because the pH of the culture solution can be adjusted without generating gas bubbles by exchanging gas.
本発明の細胞培養装置は、更に、培養液の流量を測定する流量計、培養液中の固体状の老廃物を取り除くためのフィルタ、培養液の流れを制御する集合管や分配管;培養液のpH、溶存酸素濃度、温度等をモニターするためのセンサー;培養液交換を容易にするための予備培養液貯留槽及びその流路切り替え弁、培養液サンプリングポート、運転中に基材担持手段を交換するためのバイパス切替バブル等を有していてもよい。 The cell culture device of the present invention further includes a flow meter for measuring the flow rate of the culture solution, a filter for removing solid waste in the culture solution, a collecting pipe and a distribution pipe for controlling the flow of the culture solution; Sensor for monitoring pH, dissolved oxygen concentration, temperature, etc .; Preliminary culture fluid storage tank for easy exchange of culture fluid and its flow path switching valve, culture fluid sampling port, substrate support means during operation You may have a bypass switching bubble etc. for exchange.
本発明の細胞培養装置の概念図を図3に示した。
図3に示した細胞培養装置では、培養液貯留槽8に貯留された培養液をチューブポンプ7により輸液して、脱泡手段6を通した後、基材担持手段1中の細胞が播種された三次元基材に供給する。基材担持手段1から流出した培養液は、再び培養液貯留槽8に戻される。培養液貯留槽8では、二酸化炭素含有ガスが吹き込まれ、老廃物等により変動した培養液のpHが調製される。
A conceptual diagram of the cell culture apparatus of the present invention is shown in FIG.
In the cell culture apparatus shown in FIG. 3, after the culture solution stored in the culture solution storage tank 8 is infused by the
本発明の細胞培養装置の一実施態様を示す模式図を図4に示した。
図4に示した本発明の細胞培養装置では、基材担持手段と脱泡手段(フィルタ)とを有するユニット5が6ユニット装着されており、チューブポンプ7により培養液が循環されている。細胞培養装置全体はインキュベータ9中に設置されていることから、全体の温度を極めて正確に制御することができる。
A schematic diagram showing one embodiment of the cell culture device of the present invention is shown in FIG.
In the cell culture apparatus of the present invention shown in FIG. 4, six
本発明の細胞培養装置によれば、三次元基材に播種された細胞を極めて高い効率で、しかも高密度に培養することが可能である。また、用いる三次元基材の形状及び大きさにあわせて基材担持手段を準備するだけで、種々の形状、大きさを有する三次元基材に播種された細胞を培養することができる。更に、ユニット化された基材担持手段を着脱するだけで、複数の形状等の異なる三次元基材に播種された細胞を自由に培養することができる。
本発明の細胞培養装置は、全体を一括して、又は、ユニット毎にオートクレーブ滅菌することができることから、滅菌等の保守も容易である。更に、装置全体を極めてコンパクトにまとめることができる。
According to the cell culture device of the present invention, cells seeded on a three-dimensional substrate can be cultured with extremely high efficiency and high density. Moreover, the cell seed | inoculated on the three-dimensional base material which has various shapes and magnitude | sizes can be culture | cultivated only by preparing a base material support means according to the shape and size of the three-dimensional base material to be used. Furthermore, the cells seeded on different three-dimensional substrates such as a plurality of shapes can be freely cultured simply by detaching the unitized substrate supporting means.
The cell culture device of the present invention can be sterilized or the like easily because it can be autoclaved as a whole or for each unit. Furthermore, the entire apparatus can be collected very compactly.
本発明によれば、種々の形状や大きさの三次元基材上に播種された細胞を、高い効率で、しかも高密度に培養することができる細胞培養装置を提供することができる。 ADVANTAGE OF THE INVENTION According to this invention, the cell culture apparatus which can culture | cultivate the cell seed | inoculated on the three-dimensional base material of various shapes and sizes with high efficiency and high density can be provided.
以下に実施例を掲げて本発明を更に詳しく説明するが、本発明はこれら実施例のみに限定されるものではない。 Hereinafter, the present invention will be described in more detail with reference to examples. However, the present invention is not limited to these examples.
(実施例1)
空隙部2が直径15mm、厚さ2mmの円盤状となるように図1に示したような基材担持手段1を作製し、これと孔径320μmのサポートフィルタとを組み合わせて図2に示したようなユニットを作製し、このユニットが6つ装着された図4に示した細胞培養装置を作製した。なお、細胞培養装置は、全体をインキュベータ中に置き、37℃の温度に保温した。
Example 1
As shown in FIG. 2, the base
繊維径12μmのポリグリコール酸(PGA)からなる不織布を、直径15mm、厚さ2mmの円盤状に加工し、これを三次元培養基材として、ラット骨髄未分化間葉系幹細胞約880000cellsを震盪法(12時間)により播種した。このような細胞が播種された三次元基材を5つ準備した。
細胞は、震盪播種法により基材に完全に接着させた後、各々を基材担持手段1の空隙部2中に配置して細胞培養装置に供した。
A non-woven fabric made of polyglycolic acid (PGA) having a fiber diameter of 12 μm is processed into a disk shape having a diameter of 15 mm and a thickness of 2 mm, and this is used as a three-dimensional culture substrate to shake about 880000 cells of rat undifferentiated mesenchymal stem cells. (12 hours). Five three-dimensional substrates seeded with such cells were prepared.
The cells were completely adhered to the substrate by the shaking seeding method, and then each cell was placed in the
培養液貯留槽8に貯留した培養液(α−MEM培地(インビトロジェン社製)+15%ウシ胎児血清(ハイクローン・ラボラトリーズ社製))125mLを輸液ポンプ7により分割輸液して細胞が播種された三次元基材に供給しながら、3日間培養を行った。
A tertiary solution in which 125 mL of the culture solution (α-MEM medium (manufactured by Invitrogen) + 15% fetal calf serum (manufactured by Hyclone Laboratories)) stored in the culture solution storage tank 8 is divided by the
培養終了後、各三次元基材を取り出し、その4つについてDNA定量法により三次元基材中の細胞数を測定した。結果を表1に示した。
また、三次元基材の1つをホルマリン固定した後、パラフィン包埋し、その中央部を切断した切片を作製した。この切片のヘマトキシリン−エオシン染色像を図5aに示した。図5aより、細胞は三次元基材の内部にまで均一に増殖していることが判った。
After completion of the culture, each three-dimensional substrate was taken out, and the number of cells in the three-dimensional substrate was measured for the four by a DNA quantification method. The results are shown in Table 1.
In addition, after fixing one of the three-dimensional substrates with formalin, a section was prepared by embedding in paraffin and cutting the central part. A hematoxylin-eosin stained image of this section is shown in FIG. 5a. From FIG. 5a, it was found that the cells were uniformly proliferating to the inside of the three-dimensional substrate.
(比較例1)
実施例1と同様の方法によりラット骨髄未分化間葉系幹細胞を播種した三次元基材(PGA不織布)を5つ準備した。
これらの三次元基材を、培養液(α−MEM培地(インビトロジェン社製)+15%ウシ胎児血清(ハイクローン・ラボラトリーズ社製))25mLを入れた細胞培養用100mmディッシュに個々に入れ、5%CO2、37℃に調整したインキュベータ中で3日間静置培養した。
(Comparative Example 1)
Five three-dimensional substrates (PGA non-woven fabrics) seeded with rat bone marrow undifferentiated mesenchymal stem cells were prepared in the same manner as in Example 1.
These three-dimensional substrates were individually placed in a 100 mm dish for cell culture containing 25 mL of a culture solution (α-MEM medium (manufactured by Invitrogen) + 15% fetal calf serum (manufactured by High Clone Laboratories)), and 5% The culture was stationary for 3 days in an incubator adjusted to CO 2 and 37 ° C.
培養終了後、各三次元基材を取り出し、その4つについてDNA定量法により三次元基材中の細胞数を測定した。結果を表1に示した。
また、三次元基材の1つをホルマリン固定した後、パラフィン包埋し、その中央部を切断した切片を作製した。この切片のヘマトキシリン−エオシン染色像を図5bに示した。図5bより、細胞は三次元基材の表面でのみ増殖しており、基材の内部にはほとんど侵入していないことが判った。
After completion of the culture, each three-dimensional substrate was taken out, and the number of cells in the three-dimensional substrate was measured for the four by a DNA quantification method. The results are shown in Table 1.
In addition, after fixing one of the three-dimensional substrates with formalin, a section was prepared by embedding in paraffin and cutting the central part. A hematoxylin-eosin stained image of this section is shown in FIG. 5b. From FIG. 5b, it was found that the cells grew only on the surface of the three-dimensional substrate and hardly penetrated into the substrate.
本発明によれば、種々の形状や大きさの三次元基材上に播種された細胞を、高い効率で、しかも高密度に培養することができる細胞培養装置を提供することができる。 ADVANTAGE OF THE INVENTION According to this invention, the cell culture apparatus which can culture | cultivate the cell seed | inoculated on the three-dimensional base material of various shapes and sizes with high efficiency and high density can be provided.
1 基材担持手段
2 空隙部
3 培養液流入口
4 培養液流出口
5 ユニット
6 脱泡手段
7 チューブポンプ
8 培養液貯留槽
9 インキュベータ
10 スペーサ
11 サポートフィルタ
DESCRIPTION OF
Claims (2)
細胞が接着した三次元基材を担持する手段、培養液を循環させる手段、培養液中の気泡を脱泡する手段、並びに、培養液のpH、溶存酸素濃度及び温度を調整する手段を有し、
前記細胞が接着した三次元基材を担持する手段は、ユニット化されており、複数のユニットを着脱可能とし、かつ、
前記細胞が接着した三次元基材を担持する手段は、目的とする細胞が接着した三次元基材と形状及び大きさが略同じである空隙部と、前記空隙部を挟んで両端に配置された培養液流入口と培養液流出部とを有する
ことを特徴とする細胞培養装置。 A cell culture device for culturing cells seeded on a three-dimensional substrate using a culture medium circulating in the system,
Means for supporting a three-dimensional substrate to which cells are adhered, means for circulating the culture solution, means for defoaming bubbles in the culture solution, and means for adjusting the pH, dissolved oxygen concentration and temperature of the culture solution ,
The means for supporting the three-dimensional substrate to which the cells are attached is unitized, and a plurality of units can be attached and detached, and
The means for supporting the three-dimensional substrate to which the cells are adhered is disposed at both ends with the gap portion having substantially the same shape and size as the three-dimensional substrate to which the target cell is adhered, sandwiching the gap portion. culture fluid inlet and the culture liquid outlet portion and a cell culture apparatus, comprising a.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2004029795A JP4445765B2 (en) | 2004-02-05 | 2004-02-05 | Cell culture equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2004029795A JP4445765B2 (en) | 2004-02-05 | 2004-02-05 | Cell culture equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2005218368A JP2005218368A (en) | 2005-08-18 |
JP4445765B2 true JP4445765B2 (en) | 2010-04-07 |
Family
ID=34994507
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2004029795A Expired - Fee Related JP4445765B2 (en) | 2004-02-05 | 2004-02-05 | Cell culture equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP4445765B2 (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4689383B2 (en) | 2005-07-19 | 2011-05-25 | 高木産業株式会社 | Culturing chamber, culturing apparatus, and method for feeding culture solution |
KR101738285B1 (en) * | 2007-09-19 | 2017-05-29 | 플루리스템 리미티드 | Composition for treating ischemia comprising adherent cells from placenta tissue |
DE102010064098B4 (en) * | 2010-12-23 | 2014-02-13 | Hochschule Wismar | cell reactor |
EP2920292B1 (en) * | 2012-11-13 | 2017-01-11 | Agilent Technologies, Inc. | Apparatus and methods for three-dimensional tissue measurements based on controlled media flow |
JP6758625B2 (en) * | 2014-10-31 | 2020-09-23 | 国立大学法人京都大学 | Three-dimensional culture method using biodegradable polymer and culture base material that enables cell transplantation |
CN109628304A (en) * | 2018-12-28 | 2019-04-16 | 广东省心血管病研究所 | A kind of mesenchymal stem cell culture systems |
-
2004
- 2004-02-05 JP JP2004029795A patent/JP4445765B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JP2005218368A (en) | 2005-08-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP6586407B2 (en) | Automatic tissue engineering module | |
US7906323B2 (en) | Automated bioculture and bioculture experiments system | |
JP6454314B2 (en) | Collection medium and cell collection bag for collecting mesenchymal stem cells grown in a hollow fiber bioreactor | |
JP6719387B2 (en) | Automatic cell culture and recovery device | |
US7122371B1 (en) | Modular cell culture bioreactor | |
TWI233449B (en) | High efficient cell-cultivating device | |
DK2505220T3 (en) | Method of propagating human hepatocyte-derived cells | |
CN103328625A (en) | Bioreactor | |
JP2005531300A5 (en) | ||
ES2766199T3 (en) | Frame for tissue growth in vivo | |
KR20210022162A (en) | Continuously controlled hollow fiber bioreactor | |
JP2004510431A (en) | Automated bioculture and bioculture experiment system | |
TW200302274A (en) | Cell-cultivating device | |
PT1625212E (en) | Artificial immune organ | |
JP4445765B2 (en) | Cell culture equipment | |
CN103614296A (en) | Double-chamber three-dimensional pouring bioreactor system | |
CN113846016A (en) | High-flux porous array chip, device, preparation method and application | |
KR102338639B1 (en) | Microbioreactor module | |
EP1485465A2 (en) | Microcapillary bioreactor for growth of biological tissue | |
JP2005518207A (en) | Devices and methods for culture of tissue cells | |
CN2923716Y (en) | Automatic cell culturing system | |
Pörtner et al. | Cultivation of mammalian cells in fixed-bed reactors | |
RU2789875C2 (en) | Flow-through bioreactor for cultivation of bioengineered structures | |
EP3098304A1 (en) | Hybrid cell detachment-free cell expansion system for adherent cell culturing and related proceeding protocol | |
Camacho | Development of a prototype hollow fibre bioreactor system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20070110 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20090929 |
|
A521 | Written amendment |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20091124 |
|
RD02 | Notification of acceptance of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: A7422 Effective date: 20091124 |
|
A521 | Written amendment |
Free format text: JAPANESE INTERMEDIATE CODE: A821 Effective date: 20091124 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20100112 |
|
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20100118 |
|
R150 | Certificate of patent or registration of utility model |
Ref document number: 4445765 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130122 Year of fee payment: 3 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130122 Year of fee payment: 3 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20140122 Year of fee payment: 4 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
LAPS | Cancellation because of no payment of annual fees |