JPH02142464A - Culture apparatus - Google Patents
Culture apparatusInfo
- Publication number
- JPH02142464A JPH02142464A JP29541488A JP29541488A JPH02142464A JP H02142464 A JPH02142464 A JP H02142464A JP 29541488 A JP29541488 A JP 29541488A JP 29541488 A JP29541488 A JP 29541488A JP H02142464 A JPH02142464 A JP H02142464A
- Authority
- JP
- Japan
- Prior art keywords
- culture
- air
- porous body
- culture solution
- plant cells
- 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.)
- Granted
Links
- 230000001954 sterilising effect Effects 0.000 claims description 19
- 238000004659 sterilization and disinfection Methods 0.000 claims description 13
- 239000001963 growth medium Substances 0.000 claims description 10
- 238000012258 culturing Methods 0.000 claims description 2
- 239000007788 liquid Substances 0.000 abstract description 9
- 238000000034 method Methods 0.000 abstract description 6
- 230000035755 proliferation Effects 0.000 abstract description 3
- 239000000919 ceramic Substances 0.000 abstract description 2
- 230000006835 compression Effects 0.000 abstract description 2
- 238000007906 compression Methods 0.000 abstract description 2
- 239000011521 glass Substances 0.000 abstract description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 10
- 239000001301 oxygen Substances 0.000 description 10
- 229910052760 oxygen Inorganic materials 0.000 description 10
- 229920001817 Agar Polymers 0.000 description 5
- 206010020649 Hyperkeratosis Diseases 0.000 description 5
- 239000008272 agar Substances 0.000 description 5
- 239000002609 medium Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 241000894006 Bacteria Species 0.000 description 3
- 238000009630 liquid culture Methods 0.000 description 3
- KDXKERNSBIXSRK-YFKPBYRVSA-N L-lysine Chemical compound NCCCC[C@H](N)C(O)=O KDXKERNSBIXSRK-YFKPBYRVSA-N 0.000 description 2
- KDXKERNSBIXSRK-UHFFFAOYSA-N Lysine Natural products NCCCCC(N)C(O)=O KDXKERNSBIXSRK-UHFFFAOYSA-N 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 235000015097 nutrients Nutrition 0.000 description 2
- 230000000644 propagated effect Effects 0.000 description 2
- 239000008223 sterile water Substances 0.000 description 2
- 230000001580 bacterial effect Effects 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000012136 culture method Methods 0.000 description 1
- 230000032459 dedifferentiation Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 229940088597 hormone Drugs 0.000 description 1
- 239000005556 hormone Substances 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000003756 stirring Methods 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
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/06—Nozzles; Sprayers; Spargers; Diffusers
- C12M29/08—Air lift
-
- 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
- C12M29/06—Nozzles; Sprayers; Spargers; Diffusers
-
- 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
Abstract
Description
【発明の詳細な説明】
[発明の目的]
(産業上の利用分野)
本発明は培養液を用いて植物細胞を大量に増殖させる培
養装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Object of the Invention] (Industrial Application Field) The present invention relates to a culture device for multiplying plant cells in large quantities using a culture solution.
(従来の技術)
植物体の細胞を脱分化させてカルスを誘導する一般的手
法として、例えばペトリ皿内に栄養分とホルモンを含ん
だ寒天培地を置き、この寒天培地上に植物細胞を載せて
、脱分化、増殖させてカルスを誘導する手法がある。こ
の場合、植物細胞を効率よく、脱分化、増殖させるため
に、栄養分を含んだ寒天培地を頻繁に交換する必要があ
る。(Prior art) As a general method for dedifferentiating plant cells and inducing callus, for example, an agar medium containing nutrients and hormones is placed in a Petri dish, and plant cells are placed on the agar medium. There is a method to induce callus by dedifferentiation and proliferation. In this case, in order to efficiently dedifferentiate and proliferate plant cells, it is necessary to frequently replace the agar medium containing nutrients.
また、植物体の細胞が寒天培地上で脱分化してカルスに
なった時点で、カルスを培養容器内の培養液中に移動し
て培養する液体培養手法もある。There is also a liquid culture method in which the callus is transferred to a culture solution in a culture container and cultured once the cells of the plant are dedifferentiated and become callus on an agar medium.
この場合、例えば2〜3週間の周期で寒天培地を交換し
、かつ培養液中に移動後においても、培養液中の溶融酸
素濃度を高めるために振盪したり、撹拌して培養液への
通気を実施する。In this case, for example, the agar medium is replaced every 2 to 3 weeks, and even after being transferred to the culture medium, the culture medium is aerated by shaking or stirring to increase the concentration of molten oxygen in the culture medium. Implement.
しかしながら、上記のような液体培養手法においてもま
だ解消すべき次のような問題がある。すなわち、液体培
養液中においてカルス化した植物細胞は例えば20〜3
0μmまで成長する。なお、場合によっては、5001
まで成長することもある。このような大きさまで成長し
た植物細胞は、外部から印加される側力に対して非常に
弱くなる。However, even in the liquid culture method as described above, there are still problems to be solved as follows. That is, the number of callus-formed plant cells in the liquid culture solution is, for example, 20 to 3.
Grows to 0 μm. In addition, in some cases, 5001
It may even grow to. Plant cells that have grown to such a size become extremely vulnerable to externally applied lateral forces.
したがって、前述したように培養液中の溶存酸素濃度を
高めるために培養液を振盪したり、撹拌すると、成長し
た植物細胞が破壊される問題が生じる。その結果、培養
液中にa動的に酸素を供給できなくなり、ひいては、植
物細胞を効率的に増殖できない問題が生じる。Therefore, as described above, when the culture solution is shaken or stirred in order to increase the dissolved oxygen concentration in the culture solution, the problem arises that the grown plant cells are destroyed. As a result, it becomes impossible to dynamically supply oxygen to the culture solution, which in turn causes the problem that plant cells cannot be efficiently grown.
(発明が解決しようとする課′XU)
このように、従来の培jε手法においては、増殖させよ
うとする植物細胞の培養液中の溶融酸素を植物細胞を破
壊することな(効率良く補給できなかったので、この植
物細胞が十分に増殖されない問題があった。(Problem to be solved by the invention) As described above, in the conventional culture method, the molten oxygen in the culture solution of the plant cells to be propagated can be efficiently supplied without destroying the plant cells. There was a problem that these plant cells could not be sufficiently grown.
本発明は、培養液を収納した培養容器の底壁近傍に多孔
質体を配設して、この多硬質体を介して培養液中に外部
から空気を送りこむことによって、植物細胞を破壊する
ことなく培養液中の溶解素酸素濃度を一定値以上に維持
でき、植物細胞の増殖を効率的に実施できる培養装置を
提供することを目的とする。The present invention is a method of destroying plant cells by disposing a porous body near the bottom wall of a culture container containing a culture solution and blowing air into the culture solution from the outside through this polyrigid body. It is an object of the present invention to provide a culture device that can maintain the lysin oxygen concentration in the culture solution above a certain value without any problems and can efficiently propagate plant cells.
[発明の構成〕
(課題を解決するための手段)
上記課題を解消するために本発明の培養装置におては、
植物細胞を培養する培養液を収納する培養容器と、この
培養容器内の底壁近傍に配設され、気体が通気する多孔
質体と、培養液内における多孔質体の上方位置に配設さ
れ、培養液を対流させるだめの円筒と、培養容器の底部
位置に開口し、外部から多孔質体を介して培養液内に空
気を通気させる空気供給機構と、培養容器の上部位置に
開口した空気排出機構と、空気供給機構および空気排出
機tgの各空気通路に介挿された除菌フィルタと、空気
供給機構における除菌フィルタと開口との間の空気通路
に介挿された加湿器とを備えたものである。[Structure of the Invention] (Means for Solving the Problems) In order to solve the above problems, in the culture device of the present invention,
A culture container that stores a culture medium for culturing plant cells, a porous body disposed near the bottom wall of the culture vessel through which gas passes, and a porous body disposed above the porous body within the culture medium. , a reservoir cylinder for convection of the culture solution, an air supply mechanism that opens at the bottom of the culture container and ventilates air into the culture solution from the outside through the porous body, and an air supply mechanism that opens at the top of the culture container. A discharge mechanism, a sterilization filter inserted in each air passage of the air supply mechanism and the air discharger tg, and a humidifier inserted in the air passage between the sterilization filter and the opening in the air supply mechanism. It is prepared.
(作用)
このように構成された培養装置であれば、培養液を収納
した培養容器の底壁近傍に気体が通気する多孔質体が配
設されている。そして、この多孔質体の上方位置に円筒
が配設されている。そして、空気供給機(1■でもって
多孔質体の下側から例えば圧縮ポンプ等を用いて空気を
供給すると、その空気は多孔質体で微小な気泡となって
、円筒内の培養液中を上昇する。そして、培養容器の上
方位置に開口する空気排出機構を介して外気へ排気され
る。(Function) In the culture apparatus configured as described above, a porous body through which gas is ventilated is disposed near the bottom wall of the culture container containing the culture solution. A cylinder is disposed above this porous body. Then, when air is supplied from the bottom of the porous body using an air supply device (1) using a compression pump, for example, the air becomes minute bubbles in the porous body and flows into the culture medium in the cylinder. Then, it is exhausted to the outside air through an air exhaust mechanism that opens above the culture container.
このとき、円筒内の培養液は気泡の上昇に伴って−に方
へ移動して、液面近傍に達すると円筒の外側を下降する
。すなわち、培養液は円筒の側壁を中心に対流する。な
お、除菌フィルタが空気供給機構と空気排出機構の各空
気通路に介挿されているので、培養容器内は無菌状態を
維1)!する。At this time, the culture solution in the cylinder moves in the - direction as the bubbles rise, and when it reaches near the liquid level, it descends on the outside of the cylinder. That is, the culture solution convects around the side wall of the cylinder. In addition, sterilization filters are inserted in each air passage of the air supply mechanism and air discharge mechanism, so the inside of the culture container remains sterile (1)! do.
(実施例) 以下本発明の一実施例を図面を用いて説明する。(Example) An embodiment of the present invention will be described below with reference to the drawings.
第1図は実施例の培養装置を示す断面模式図である。1
はガラス等でa底円筒状に形成された培養容器である。FIG. 1 is a schematic cross-sectional view showing a culture apparatus of an example. 1
is a culture container made of glass or the like and formed into an A-bottom cylindrical shape.
この培養容器1内に植物細胞を増殖させるだめの培養液
2が収納される。そして、培養容器1の底壁1aJ&:
傍は小径に形成されており、この小径部1bの上端に円
盤状の多孔質体3が在人固定されている。この多孔質体
3は、例えば、セラミックス、焼結金属、フッ素樹脂フ
ィルタ等で形成されており、一方の面から加圧した空気
を加えると、空気が多孔質体3内に存在する微小な間隙
を通過して反対面側へ抜ける性質を釘する。A culture solution 2 for growing plant cells is stored in this culture container 1. Then, the bottom wall 1aJ of the culture container 1 &:
The side portion is formed to have a small diameter, and a disc-shaped porous body 3 is fixed to the upper end of this small diameter portion 1b. This porous body 3 is made of, for example, ceramics, sintered metal, a fluororesin filter, etc., and when pressurized air is applied from one side, the air fills the minute gaps existing in the porous body 3. The property of passing through and exiting to the opposite side is nailed.
その多孔質体3の上方位置に軸心が上下方向を向く円筒
4が図示しない支持部材にて培養容器1に支14jされ
ている。そして、培養容器1の蓋体】Cの中央位置に培
養すべき植物細胞を投入するだめの植付口5が形成され
ている。また、蓋体ICには、空気排出機構としての排
気管6が取付けられている。そして、この排気管6の中
途位置に培養容器1内へ大気中の雑菌が侵入するのを防
止するための除菌フィルタ7aが介挿されている。At a position above the porous body 3, a cylinder 4 whose axis is oriented in the vertical direction is supported 14j on the culture container 1 by a support member (not shown). A planting port 5 for introducing plant cells to be cultured is formed in the center of the lid C of the culture container 1. Further, an exhaust pipe 6 as an air exhaust mechanism is attached to the lid IC. A sterilization filter 7a is inserted in the middle of the exhaust pipe 6 to prevent bacteria in the atmosphere from entering the culture container 1.
また、培養容器1の底壁1aには給気管8aの一端が開
口しており、この給気管8aの他端は無菌水9が封入さ
れた加湿器10内に開口している。Further, one end of an air supply pipe 8a is opened in the bottom wall 1a of the culture container 1, and the other end of this air supply pipe 8a is opened into a humidifier 10 in which sterile water 9 is sealed.
さらに別の給気管8bの一端が加湿器10内の無菌水9
内に開口しており、この給気管8bの他端は除菌フィル
タ7bおよび加圧ポンプ11を介して外気に開口してい
る。しかして、給気管8a。Furthermore, one end of another air supply pipe 8b is connected to the sterile water 9 in the humidifier 10.
The other end of this air supply pipe 8b is opened to the outside air via a sterilization filter 7b and a pressurizing pump 11. Therefore, the air supply pipe 8a.
8bおよび加圧ポンプ11は空気供給機構を構成する。8b and the pressurizing pump 11 constitute an air supply mechanism.
また、培養容器1の蓋体IC近傍位置には、給液管12
の一端が開口しており、給液管12の他端はポンプ13
を介して予備の培養液2を収納する培養液供給タンク1
4内の培養液2内に開口している。そして、この培養液
供給タンク14には、除菌フィルタ7Cが設けられた空
気抜き管15が取付けられている。In addition, a liquid supply pipe 12 is located near the lid IC of the culture container 1.
One end is open, and the other end of the liquid supply pipe 12 is connected to the pump 13.
A culture solution supply tank 1 that stores a spare culture solution 2 via the
It opens into the culture medium 2 in 4. An air vent pipe 15 equipped with a sterilization filter 7C is attached to this culture solution supply tank 14.
さらに、培養容器1の前記多孔質体3近傍の側壁には培
養容器1内の培養液2を排出するための排液管16が取
付けられている。なお、排液管16には弁17が取付け
られている。Further, a drain pipe 16 is attached to the side wall of the culture container 1 near the porous body 3 for draining the culture solution 2 in the culture container 1. Note that a valve 17 is attached to the drain pipe 16.
このように構成された培養装置でもって、植物細胞を増
殖させる場合、まず最初に、ポンプ13を駆動して培養
液供給タンク14内の培養液2を、給液管12を介して
、液面が円筒4の上端位置より上方に上昇するまで培養
容器1内へ供給する。When growing plant cells using the culture apparatus configured as described above, first, the pump 13 is driven to supply the culture solution 2 in the culture solution supply tank 14 via the solution supply pipe 12 to the liquid level. is fed into the culture container 1 until it rises above the upper end position of the cylinder 4.
次に、増殖すべき植物細胞を植付口5から培養液2内へ
投入する。Next, plant cells to be propagated are introduced into the culture solution 2 through the planting port 5.
次に、加圧ポンプ11を起動して、外気の空気を除菌フ
ィルタ7bおよび加湿器10を経由して培養容器1内の
多孔質体3の下面に供給する。なお、多孔質体3の下面
に到達した空気は、除菌フィルタ7bで空気中に含まれ
る細菌が除去されて無菌状態になる。さらに、除湿器1
0によって多孔質体3の下面に加圧される空気の湿度は
ほぼ限界湿度まで上昇されている。Next, the pressure pump 11 is activated to supply outside air to the lower surface of the porous body 3 in the culture container 1 via the sterilizing filter 7b and the humidifier 10. Note that the air that has reached the lower surface of the porous body 3 is sterilized by removing bacteria contained in the air by the sterilization filter 7b. Furthermore, dehumidifier 1
The humidity of the air pressurized to the lower surface of the porous body 3 is increased to almost the limit humidity.
加圧ポンプ11で多孔質体3の下面に加圧された空気は
、この多孔質体3内の微小間隙を通って多孔質体3の上
面へ出る。そして、微小な気泡18となって円筒4内の
培養液2巾を水面に向かって上昇する。水面から飛出た
気泡18の空気は蓋体1cに開口する排気管6および除
菌フィルタ7aを介して大気へ放出される。Air pressurized to the lower surface of the porous body 3 by the pressurizing pump 11 passes through minute gaps within the porous body 3 and exits to the upper surface of the porous body 3. Then, they become minute bubbles 18 and rise two widths of the culture solution in the cylinder 4 toward the water surface. The air in the bubbles 18 flying out from the water surface is released into the atmosphere through the exhaust pipe 6 and the sterilization filter 7a that open in the lid 1c.
そして、円筒4内に存在する培養液2は、図中矢印で示
すように、気泡18の上昇に伴って上昇し、液面近傍で
円筒4の外側へ移動して、円筒4の外側を下方へ移動す
る。そして、円筒4の下側を通過して、円筒4内へ入り
、気泡18にて再び上昇する。すなわち、培養液2は円
筒4の側壁を中心に対流する。Then, the culture solution 2 existing in the cylinder 4 rises as the bubbles 18 rise, as shown by the arrow in the figure, moves to the outside of the cylinder 4 near the liquid level, and moves downward on the outside of the cylinder 4. Move to. Then, it passes under the cylinder 4, enters the cylinder 4, and rises again at the bubble 18. That is, the culture solution 2 convects around the side wall of the cylinder 4.
このように、培養容器1内に収納された培養液2内には
酸素を含んだ微小の気泡18が通気するので、培養液2
中に酸素が十分補給され、培養液2中の溶解酸素濃度は
ほぼ一定水準に維持される。In this way, the microscopic air bubbles 18 containing oxygen are vented into the culture solution 2 stored in the culture container 1, so that the culture solution 2
Oxygen is sufficiently supplied inside the culture solution 2, and the dissolved oxygen concentration in the culture solution 2 is maintained at a substantially constant level.
さらに、培養液2は円筒4を中心に対流するので、酸素
が均一に供給される。また、対流によって、培養液2中
に投入された増殖すべき植物細胞が培養容器1内の下部
位置に留まることなく、培養液2中に均等に分散する。Furthermore, since the culture solution 2 convects around the cylinder 4, oxygen is uniformly supplied. In addition, due to the convection, the plant cells to be proliferated that have been introduced into the culture solution 2 do not remain in the lower part of the culture container 1, but are evenly dispersed in the culture solution 2.
したがって、培養液2中に投入された植物細胞が最良の
条件下で効率よく増殖される。Therefore, the plant cells introduced into the culture solution 2 are efficiently grown under the best conditions.
また、培養液2中には微小な気泡18が通るのみである
ので、成長した植物細胞に過大な剪断応力が印加される
ことはないので、成長過程で破壊されることはない。Further, since only minute air bubbles 18 pass through the culture solution 2, excessive shear stress is not applied to the grown plant cells, so that they are not destroyed during the growth process.
また、加湿器10を用いて多孔質体3を経由して培養液
2内に供給される空気の湿度を限界湿度まで上昇させて
いるので、乾燥空気を使用した場合における水蒸気とし
て蒸発して排気管6を介して外気へ放出される培養液を
抑制できる。すなわち、培養液2の液量減少および液濃
度変化を防止できる。よって、植物細胞の増殖をさらに
最良の条件で実行できる。In addition, since the humidifier 10 is used to increase the humidity of the air supplied into the culture medium 2 via the porous body 3 to the limit humidity, when dry air is used, it evaporates as water vapor and is exhausted. It is possible to suppress the culture solution being released into the outside air through the tube 6. That is, a decrease in the volume of the culture solution 2 and a change in the concentration of the culture solution 2 can be prevented. Therefore, plant cells can be grown under even better conditions.
また、培養容器1内と外気とを連通する容管6゜8b、
15には除菌フィルタ7a、7b、7cが介挿されてい
るので、大気中の雑菌が培養容器l内へ侵入することが
防止される。In addition, a container tube 6°8b that communicates the inside of the culture container 1 with the outside air,
Since the sterilization filters 7a, 7b, and 7c are inserted in the filter 15, germs in the atmosphere are prevented from entering the culture container l.
また、加湿器10を除菌フィルタ7bと多孔質体3との
間の空気通路に介挿しているので、除菌フィルタ7bが
濡れることを防止でき、フィルタの目づまり、雑菌増殖
を抑制でき、除菌フィルタ7bの除菌機能を長期間に亘
って持続させることが可能となる。すなわち、除菌フィ
ルタ7bの寿命を長くできる。In addition, since the humidifier 10 is inserted into the air passage between the sterilizing filter 7b and the porous body 3, it is possible to prevent the sterilizing filter 7b from getting wet, and to suppress clogging of the filter and proliferation of various bacteria. It becomes possible to maintain the sterilization function of the sterilization filter 7b for a long period of time. In other words, the life of the sterilizing filter 7b can be extended.
[発明の効果]
以上説明したように本発明の培養装置によれば、培養液
を収納した培養容器の底壁近傍に多孔質体を配設して、
この多硬質体を介して培養液中に外部から空気を送りこ
むようにしている。したがって、植物細胞を破壊するこ
となく培養液中の溶解素酸素濃度を一定値以上に維持で
き、植物細胞の増殖を効率的に実施できる。また、加湿
器を除菌フィルタの空気流路の下流側に配設することに
よって、除菌フィルタを長寿命化できる。[Effects of the Invention] As explained above, according to the culture device of the present invention, a porous body is disposed near the bottom wall of a culture container containing a culture solution,
Air is introduced from the outside into the culture solution through this multi-hard body. Therefore, the lysin oxygen concentration in the culture solution can be maintained above a certain value without destroying the plant cells, and the plant cells can be efficiently grown. Further, by disposing the humidifier downstream of the air flow path of the sterilizing filter, the life of the sterilizing filter can be extended.
第1図は本発明の一実施例に係わる培養装置を示す断面
模式図である。
1・・・培養容器、2・・・培養液、3・・・多孔質体
、4・・・円筒、6・・・排気管、7 a r 7
b r 7 c・・・除菌フィルタ、8a、8b・・
・給気管、10・・・加湿器、11・・・加圧ポンプ、
14・・・培養液供給タンク。FIG. 1 is a schematic cross-sectional view showing a culture apparatus according to an embodiment of the present invention. DESCRIPTION OF SYMBOLS 1...Culture container, 2...Culture solution, 3...Porous body, 4...Cylinder, 6...Exhaust pipe, 7 a r 7
b r 7 c...Bacterial filter, 8a, 8b...
・Air supply pipe, 10... Humidifier, 11... Pressure pump,
14...Culture solution supply tank.
Claims (1)
培養容器内の底壁近傍に配設され、気体が通気する多孔
質体と、前記培養液内における前記多孔質体の上方位置
に配設され、前記培養液を対流させるための円筒と、前
記培養容器の底部位置に開口し、外部から前記多孔質体
を介して前記培養液内に空気を通気させる空気供給機構
と、前記培養容器の上部位置に開口した空気排出機構と
、前記空気供給機構および空気排出機構の各空気通路に
介挿された除菌フィルタと、前記空気供給機構における
前記除菌フィルタと前記開口との間の空気通路に介挿さ
れた加湿器とを備えた培養装置。A culture container that stores a culture medium for culturing plant cells, a porous body disposed near the bottom wall of the culture vessel through which gas passes, and a porous body disposed above the porous body within the culture medium. a cylinder provided therein for causing convection in the culture solution; an air supply mechanism that opens at a bottom position of the culture container and aerates air into the culture solution from the outside through the porous body; and the culture container. an air discharge mechanism opened at an upper position; a sterilization filter inserted into each air passage of the air supply mechanism and the air discharge mechanism; and air between the sterilization filter and the opening in the air supply mechanism. A culture device equipped with a humidifier inserted in a passage.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29541488A JPH0697992B2 (en) | 1988-11-22 | 1988-11-22 | Incubator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29541488A JPH0697992B2 (en) | 1988-11-22 | 1988-11-22 | Incubator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02142464A true JPH02142464A (en) | 1990-05-31 |
JPH0697992B2 JPH0697992B2 (en) | 1994-12-07 |
Family
ID=17820298
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP29541488A Expired - Lifetime JPH0697992B2 (en) | 1988-11-22 | 1988-11-22 | Incubator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0697992B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100369240B1 (en) * | 2000-04-07 | 2003-01-24 | 환인제약 주식회사 | Bioreactor for the culture of microorganisms |
JP2011115153A (en) * | 2009-10-27 | 2011-06-16 | Takara Bio Inc | Method for producing lyophyllum ulmarium fruiting body |
-
1988
- 1988-11-22 JP JP29541488A patent/JPH0697992B2/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100369240B1 (en) * | 2000-04-07 | 2003-01-24 | 환인제약 주식회사 | Bioreactor for the culture of microorganisms |
JP2011115153A (en) * | 2009-10-27 | 2011-06-16 | Takara Bio Inc | Method for producing lyophyllum ulmarium fruiting body |
Also Published As
Publication number | Publication date |
---|---|
JPH0697992B2 (en) | 1994-12-07 |
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