JPH02219565A - Cell culture device - Google Patents
Cell culture deviceInfo
- Publication number
- JPH02219565A JPH02219565A JP3939489A JP3939489A JPH02219565A JP H02219565 A JPH02219565 A JP H02219565A JP 3939489 A JP3939489 A JP 3939489A JP 3939489 A JP3939489 A JP 3939489A JP H02219565 A JPH02219565 A JP H02219565A
- Authority
- JP
- Japan
- Prior art keywords
- culture
- gap
- cell culture
- lid
- culture device
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000004113 cell culture Methods 0.000 title claims abstract description 19
- 230000000694 effects Effects 0.000 abstract description 11
- 238000009423 ventilation Methods 0.000 abstract description 6
- 239000001963 growth medium Substances 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 14
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- 239000002609 medium Substances 0.000 description 6
- 238000005273 aeration Methods 0.000 description 4
- 238000005259 measurement Methods 0.000 description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 230000007774 longterm Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 239000013543 active substance Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000012258 culturing Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 102000008186 Collagen Human genes 0.000 description 1
- 108010035532 Collagen Proteins 0.000 description 1
- 102000016359 Fibronectins Human genes 0.000 description 1
- 108010067306 Fibronectins Proteins 0.000 description 1
- 239000012980 RPMI-1640 medium Substances 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 229920001436 collagen Polymers 0.000 description 1
- 230000005757 colony formation Effects 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940088597 hormone Drugs 0.000 description 1
- 239000005556 hormone Substances 0.000 description 1
- 230000009545 invasion Effects 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 230000035899 viability Effects 0.000 description 1
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
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/02—Form or structure of the vessel
- C12M23/10—Petri dish
-
- 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
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/38—Caps; Covers; Plugs; Pouring means
-
- 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
Landscapes
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Chemical & Material Sciences (AREA)
- Zoology (AREA)
- Wood Science & Technology (AREA)
- Sustainable Development (AREA)
- Microbiology (AREA)
- Biotechnology (AREA)
- Biomedical Technology (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Clinical Laboratory Science (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、細胞の培養性を高めた細胞培養器に関するも
のである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a cell culture device with improved cell culturability.
細胞の培養技術は現在産業上で頻繁に利用され活
ており、薬物やホルモン、抗体等の生理活性物質が生産
されている。これらの大量培養の前段階である細胞培養
の際の細胞培養器の培養性も、効率化のためには非常に
重要である。Cell culture technology is currently frequently used and utilized in industry, and physiologically active substances such as drugs, hormones, and antibodies are produced. The cultivability of the cell culture vessel during cell culture, which is a preliminary stage of mass culture, is also very important for efficiency.
従来、小規模の培養器はシャー曇ルチウェルプレート等
が用いられている。これらは、細胞培養器の培養性を高
めるためには、培養面をコラーゲンやフィブロネクチン
等の生理活性物質で覆う方法や、特殊な表面処理を行う
等の方法が提案されている。しかし、これらは特別な手
法や技術を必要としているため、−殻内な培養器に適用
することは困難である。Conventionally, a Shear cloud multiwell plate or the like has been used as a small-scale culture vessel. In order to improve the culturability of cell culture vessels, methods such as covering the culture surface with physiologically active substances such as collagen and fibronectin, and performing special surface treatments have been proposed. However, these methods require special methods and techniques and are therefore difficult to apply to in-shell culture vessels.
また、これらの培養器は上面が開放された容器を雑菌の
侵入を防ぐふたで覆った構造を有している。培養は37
℃の培養槽中で行い、また、培地中のpHの変化を防ぐ
ための炭酸ガスの存在下湿度100%調整の中で行われ
る。そのため、培養器の外部との通気を保つため、ふた
と容器本体との間に間隙が設けられているのが一般的で
ある。Furthermore, these culture vessels have a structure in which a container with an open top is covered with a lid to prevent invasion of germs. Culture is 37
The culture is carried out in a culture tank at 100°C, and the humidity is adjusted to 100% in the presence of carbon dioxide gas to prevent changes in the pH in the culture medium. Therefore, in order to maintain ventilation with the outside of the incubator, a gap is generally provided between the lid and the container body.
本発明は、細胞培養器の培養性をより高めるために、培
!に器の構造に着目してその構成について検討を行なっ
た結果、培養容器本体とふたとの間の外気との流通可能
な間隙と培養面積との関係が、培養性に重大な影響を有
することを見い出し、更に検討を繰り返すことにより本
発明を完成させたもので、その目的とするところは、細
胞の培養性を著しく高めた細胞培養器を提供することに
あり、細胞を利用する際の効率を高めることにより、そ
の応用及び利用を促進することにある。The present invention aims to improve the culturability of cell culture vessels. As a result of studying the structure of the vessel, we found that the relationship between the culture area and the gap between the culture vessel body and the lid that allows for passage of outside air has a significant impact on cultivability. The present invention has been completed by discovering the The aim is to promote its application and utilization by increasing its effectiveness.
本発明は、培養面の上面が開放可能な細胞培養器であっ
て、上面を覆うふたと本体との間の外気との流通可能な
間隙の断面積(G)と培養器の培養面積(A)の比A/
Gが150〜1000の範囲にあることを特徴とする細
胞培養器である。The present invention is a cell culture device whose top surface can be opened, and the cross-sectional area (G) of the gap between the lid covering the top surface and the main body through which outside air can flow, and the culture area (A ) ratio A/
This cell culture vessel is characterized in that G is in the range of 150 to 1000.
本発明における培養面の上面が開放可能な細胞培養器と
は、−船釣な容器にふたをすることにより培養器を構成
したもので、シャーレやマルチウェルプレート等が代表
的である。これらは、培養の際に外部との通気を保つ間
隙を有している。In the present invention, the cell culture vessel whose top surface can be opened is a culture vessel constructed by covering a container with a lid, and is typically a petri dish, a multiwell plate, or the like. These have gaps that maintain ventilation with the outside during culture.
この培養の際の外部との通気は、内部への酸素の供給を
行う他、炭酸ガスの通気により炭酸ガス濃度を一定に保
ち、培地のpHを一定に保つ働きをする。しかしその反
面、培地の蒸発による減少を招く等の逆の作用も持つ、
この作用はあまり顧りみられなかったが、詳しい検討の
結果、培養性への効果が大きく、この通気を制御するこ
とにより培養性を高めることが可能であった。This aeration with the outside during culturing not only supplies oxygen to the inside, but also serves to keep the carbon dioxide concentration constant and the pH of the medium constant by aeration of carbon dioxide gas. However, on the other hand, it also has the opposite effect, such as causing a decrease due to evaporation of the medium.
Although this effect has not been given much attention, detailed studies have shown that it has a large effect on culturability, and it is possible to improve culturability by controlling this aeration.
この通気の状態は、培養器の容器本体とふたとの嵌合に
よる間隙の大きさによって決まり、また、培養性への効
果はこの培養器の培養面積との比により表わすことがで
きる。この比は間隙の断面積(G)と培養面積(A)の
比A/Gとして表わされる。この値が大きいほど通気が
少ないことを示し、培養性への効果も高いが、値が非常
に大きいと密封培養と同じになり、長期間の培養の際に
は、酸素の供給が不足するため好ましくなく、数日から
数週間の培養期間では150〜1000の範囲が適切で
ある。The state of this ventilation is determined by the size of the gap created by the fit between the container body and the lid of the incubator, and the effect on culture performance can be expressed by the ratio to the culture area of the incubator. This ratio is expressed as the ratio A/G of the cross-sectional area of the gap (G) and the culture area (A). The larger this value is, the less aeration is, and the effect on cultivability is also high; however, if the value is very large, it will be the same as sealed culture, and during long-term culture, oxygen supply will be insufficient. This is not preferred, and a range of 150 to 1000 is appropriate for a culture period of several days to several weeks.
また、この効果は一般的な培養器において見られる特性
であるが、多数のウェルが集まった構造ヲ持つ96.4
B、24ウエル等のマルチウェルプレートにおいて、そ
の効果は更に顕著である。Additionally, this effect is a characteristic seen in general culture vessels, but 96.4
B. In multi-well plates such as 24 wells, the effect is even more remarkable.
以下、実施例により本発明を説明する。The present invention will be explained below with reference to Examples.
各種の培養面積(A)と通気のための間隙(G)を有す
るマルチウェルプレート及びシャーレを作成した。それ
ぞれ細胞培養用として調整し、T線滅菌を行なった後、
培地の蒸発性および培養性の試験に供した。試験に用い
た培養器は第1表に示した通りで、蒸発性および培養性
の試験方法は次の通りとした。Multiwell plates and petri dishes having various culture areas (A) and gaps for ventilation (G) were prepared. After preparing each for cell culture and performing T-ray sterilization,
The medium was tested for evaporability and culturability. The incubator used in the test was as shown in Table 1, and the test methods for evaporability and culturability were as follows.
蒸発性の測定方法
各容器毎に規定量の純水を分注し、湿度調整のないイン
キュベーターと、湿度100%に調整したインキュベー
ターにそれぞれ静置した後、残留した純水の量を測定し
て、残留率(%)を求めた。Method for measuring evaporation: Dispense a specified amount of pure water into each container, leave them in an incubator without humidity adjustment, and in an incubator adjusted to 100% humidity, then measure the amount of pure water remaining. , the residual rate (%) was determined.
ウェル数の多いプレートでは、外周部を内側部で蒸発性
が異なるため別に測定を行った。測定結果を第2表およ
び第3表に示した。For plates with a large number of wells, measurements were performed separately for the outer periphery and the inner part because the evaporation properties differed. The measurement results are shown in Tables 2 and 3.
培養性の測定方法
培養性の評価のために、プレートエフィシエンシイ法(
PE法)とりミティングダイリューシジン法(LD法)
を行った。測定結果は第4表に示した通り。Method for measuring culturability To evaluate culturability, the plate efficiency method (
PE method) Torimiting dileucidin method (LD method)
I did it. The measurement results are shown in Table 4.
・プレートエフ諺シンシイ法(PE法)細胞はHeLa
、培地はMEM+10%CSを使用した。各容器に規定
量の細胞数を播種し、約lO日間の培養後に、培養面に
、生成したコロニーの数を数え、播種細胞数との比を求
めてプレートエフiンシイ(PE)とした。・Plate E Proverb Shinshii method (PE method) Cells are HeLa
The medium used was MEM + 10% CS. A specified amount of cells were seeded in each container, and after culturing for about 10 days, the number of colonies formed was counted on the culture surface, and the ratio to the number of seeded cells was determined as plate efficiency (PE).
・リミティ→ングダイリエーシッン法(LD法)細胞は
N5−1、培地はRPMI−1640+10%FC3を
使用した。各容器(48ウエル又は96ウエル)に規定
の細胞濃度にて播種を行い、コロニーを生成したウェル
の数を数え、全ウェルに対する播種細胞数との比を求め
てコロニー生成率とした。・Limity→Ningalyzing method (LD method) N5-1 cells were used, and RPMI-1640+10% FC3 was used as the medium. Cells were seeded at a specified concentration in each container (48 wells or 96 wells), the number of wells in which colonies were formed was counted, and the ratio of the number of seeded cells to all wells was determined as the colony production rate.
尚、PE及びコロニー生成率は、播種した細胞の中の何
%が実際に増殖したかを示す数値で、細胞種や培養条件
により異なるが、本測定条件では60%〜70%程度が
最大である。In addition, PE and colony production rate are numerical values that indicate what percentage of the seeded cells actually proliferated, and although they vary depending on the cell type and culture conditions, under these measurement conditions, the maximum is about 60% to 70%. be.
培養面積(A)と間隙CG)の比(A/G比)と、培地
の蒸発性との関係では、湿度調整のないインキュベータ
ー中で測定した残留率に明確に相関が表れ、A/G比が
高い容器はど残留率が高い。Regarding the relationship between the ratio of the culture area (A) to the gap CG (A/G ratio) and the evaporability of the medium, there is a clear correlation with the residual rate measured in an incubator without humidity adjustment, and the A/G ratio Containers with high levels of residual water have a high residual rate.
実際に培養を行う湿度100%調整のインキュベーター
では、長期間のインキュベーターの外側ウェルについて
差異が表れる。In an incubator with 100% humidity control in which culture is actually performed, differences appear in the outer wells of long-term incubators.
これらの特性は細胞の培養性に影響を与え、Al6比が
小さい容器(N114.7.8.9.10.11)では
、プレートエフ?シンシイ又はコロニー生成率が小さく
なる。A/Gの比が150以上の試料(Nlll、2.
3.5.6)で、培養性が高まり、プレートエフ穴ンシ
イ又はコロニー生成率が60%程度以上の高い数値を示
す。These characteristics affect the culturability of cells, and in containers with a low Al6 ratio (N114.7.8.9.10.11), PlateF? The colony formation rate becomes smaller. Samples with an A/G ratio of 150 or more (Nllll, 2.
3.5.6), the culturability is improved and the plate efficiency or colony production rate shows a high value of about 60% or more.
これらの効果は、シャーレ等でも見られるが、マルチウ
ェルプレート類でその効果は特に著しい。Although these effects can be seen in petri dishes, the effects are particularly remarkable in multiwell plates.
また、A/Gの比が1000以上の培養器(阻13)は
、密封培養に近く通気は非常に少なくなそのため、
培養性は高くな(、
また長期間の
〔発明の効果〕
本発明に従うと、培養性に優れた細胞培養器を容易に作
成することができ、また細胞の培養性や生存性が再現よ
(得られ、細胞の培養用容器として最適な性能を有する
細胞培養器を提供することができる。In addition, an incubator with an A/G ratio of 1000 or more (13) is close to a sealed culture and has very little ventilation, so it has high cultivability (also, long-term [effects of the invention]) according to the present invention. It is possible to easily create a cell culture vessel with excellent culturability, and the culturability and viability of cells can be reproduced (obtained, providing a cell culture vessel with optimal performance as a cell culture vessel. can do.
Claims (1)
上面を覆うふたと本体との間の外気との流通可能な間隙
の断面積(G)と培養器の培養面積(A)の比A/Gが
150〜1000の範囲にあることを特徴とする細胞培
養器。(1) A cell culture device with an open top culture surface,
It is characterized in that the ratio A/G of the cross-sectional area (G) of the gap between the lid covering the top surface and the main body through which outside air can circulate and the culture area (A) of the incubator is in the range of 150 to 1000. Cell culture vessel.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3939489A JPH02219565A (en) | 1989-02-21 | 1989-02-21 | Cell culture device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3939489A JPH02219565A (en) | 1989-02-21 | 1989-02-21 | Cell culture device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02219565A true JPH02219565A (en) | 1990-09-03 |
Family
ID=12551783
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3939489A Pending JPH02219565A (en) | 1989-02-21 | 1989-02-21 | Cell culture device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02219565A (en) |
-
1989
- 1989-02-21 JP JP3939489A patent/JPH02219565A/en active Pending
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