JPH02276566A - Apparatus for culturing plant cell - Google Patents
Apparatus for culturing plant cellInfo
- Publication number
- JPH02276566A JPH02276566A JP9970189A JP9970189A JPH02276566A JP H02276566 A JPH02276566 A JP H02276566A JP 9970189 A JP9970189 A JP 9970189A JP 9970189 A JP9970189 A JP 9970189A JP H02276566 A JPH02276566 A JP H02276566A
- Authority
- JP
- Japan
- Prior art keywords
- culture
- culture solution
- cell
- sieve
- vessel
- 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
- 238000012258 culturing Methods 0.000 title claims abstract description 6
- 210000004027 cell Anatomy 0.000 abstract description 32
- 238000007664 blowing Methods 0.000 abstract description 4
- 238000003756 stirring Methods 0.000 abstract description 3
- 210000004748 cultured cell Anatomy 0.000 abstract description 2
- 230000035755 proliferation Effects 0.000 abstract description 2
- 238000010276 construction Methods 0.000 abstract 1
- 238000004113 cell culture Methods 0.000 description 5
- 239000007789 gas Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000004677 Nylon Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229920001778 nylon Polymers 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 230000010261 cell growth Effects 0.000 description 1
- 230000004663 cell proliferation Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000001963 growth medium Substances 0.000 description 1
- 239000002609 medium Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000013587 production medium Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000013076 target substance Substances 0.000 description 1
Landscapes
- 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〕
本発明は植物細胞培養装置に関し、さらに詳しくは異な
るサイズの細胞集塊に分級することができる植物細胞培
養装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a plant cell culture device, and more particularly to a plant cell culture device capable of sorting into cell aggregates of different sizes.
植物培養細胞を用いて有用物質を生産させる場合、一般
に細胞の増殖条件と有用物質生産条件が異なることが多
く、2段培養が用いられている。When producing useful substances using cultured plant cells, the cell growth conditions and the useful substance production conditions are often different, and two-stage culture is used.
2段培養は第5図に示すように、1段目培養槽で細胞の
増殖に適した条件であらかじめ増殖させた細胞を、次に
2段目培養槽9に移し、生産に適した条件のもとで培養
し、目的とする有用物質を生産する方法である。なお、
図中3は増殖培地、5は攪拌翼、7は生産培地を示す、
1段目の培養で増殖させた細胞は、一般に細胞同士が数
個〜数百個集まった集塊を形成する。この細胞集塊のサ
イズ(大きさ)によって、有用物質の生産能が異なるこ
とが幾つかの植物細胞で知られている。例えば、AoM
、KinnersI!、eyらは、ニンジン(Dauc
us carota L+)の培養細胞からアンド
シアニンを生産させる培養において、63μm以下の集
塊の方が170μm以上の集塊よりも生産能が高いこと
を報告している(A。In two-stage culture, as shown in Figure 5, cells that have been grown in advance in the first-stage culture tank under conditions suitable for cell proliferation are then transferred to the second-stage culture tank 9, where they are grown under conditions suitable for production. This is a method to produce the target useful substance by cultivating the target substance. In addition,
In the figure, 3 indicates the growth medium, 5 indicates the stirring blade, and 7 indicates the production medium.
The cells grown in the first stage of culture generally form clusters of several to several hundred cells. It is known that the ability of some plant cells to produce useful substances differs depending on the size of this cell aggregate. For example, AoM
, KinnersI! , ey et al.
In culturing andocyanin production from cultured cells of P. carota L+), it has been reported that agglomerates with a diameter of 63 μm or less have higher productivity than agglomerates with a diameter of 170 μm or more (A).
M、Kinnersfey et al、、F”1
anta、149.200−204 (1980))。M,Kinnersfey et al,,F”1
anta, 149.200-204 (1980)).
このような場合、第6図のように1段目の培養において
、増殖させた細胞を培養槽1から一度全部抜出し、これ
をナイロンまたはステンレスのふるい15にかけ、希望
するサイズの集塊11のみを2段目の培養槽9に移す方
法が考えられる。In such a case, as shown in FIG. 6, in the first stage of culture, all the grown cells are removed from the culture tank 1, passed through a nylon or stainless steel sieve 15, and only the aggregates 11 of the desired size are removed. A possible method is to transfer it to the second stage culture tank 9.
13は目的とするサイズ以下の細胞集塊である。13 is a cell aggregate smaller than the target size.
しかしこの方法では、細胞を一旦培養槽の外に出さなけ
ればならず、雑菌汚染等の影響が懸念される。However, with this method, the cells must be taken out of the culture tank, and there are concerns about the effects of bacterial contamination.
[発明が解決しようとする課題〕
本発明の目的は、上記従来技術の課題を解決し、単一の
装置で効率よく、ジ−ブトカルチャーを行うことができ
る植物細胞培養装置を提供することにある。[Problems to be Solved by the Invention] An object of the present invention is to solve the above-mentioned problems of the prior art and to provide a plant cell culture device that can efficiently perform jibut culture with a single device. be.
本発明は、培養槽と、該培養槽内に培養液を流通させる
手段と、該培養槽内の培養液の流路を遮るように設けら
れた1以上のふるいと、該ふるいによって分級された細
胞集塊を槽外にそれぞれ取り出す手段とを有することを
特徴とする。The present invention provides a culture tank, a means for circulating a culture solution in the culture tank, one or more sieves provided so as to block the flow path of the culture solution in the culture tank, and a cell classified by the sieve. It is characterized by having means for taking out each cell aggregate out of the tank.
〔実施例〕
本発明の実施例を図面により説明する。第1図〜第3図
は本発明装置およびその操作手順を示した説明図である
。[Example] An example of the present invention will be described with reference to the drawings. 1 to 3 are explanatory diagrams showing the apparatus of the present invention and its operating procedure.
第1図に示した装置は、培養槽20と、その上部に設け
られた培養液の供給管39と、該培養槽20内の培養液
の流路(上下方向)に順次間隔をおいて設けられた第1
ふるい21および第2ふるい23と、培養槽の底部に挿
入されたガス吹込管31と、前記第1ふるい21上およ
び第2ふるい23上の細胞集塊貯溜箇所に設けられた細
胞集塊の取出し管35.37と、培養槽底部に設けられ
た同様な取出し管33とからなる。第1図において、例
えば1段目の培養で1〜2mmのサイズの細胞集塊の置
数を目的とするとき、第1ふるい21としては2閣のメ
ツシュ、第2ふるい23として1mo+のメツシュを培
養槽20に取付け、ガス吹込み管31からガス(空気、
酸素、窒素等)を供給し、撹拌を行う。培養を続けると
2 mm以上になった細胞集塊25の大部分は培養槽内
の第1ふるい21の上に、また1mm以下の細胞集塊2
9の大部分は培養槽の下部に集まり、また目的とする1
〜2mの集塊27は培養槽の中間の第2ふるい23上に
集まる。ふるい(以下メツシュともいう)の材質はナイ
ロン、ステンレス等、耐久性のあるものであればよいが
、培養槽を滅菌するため熱に強いものが好ましい。また
メツシュのサイズ、取付は位置は特に制約はない、ただ
し、目的とするサイズ部分の容積は、小さい方がより集
塊の分級効率はよい。メツシュは図に示すように勾配を
持って取付けた方が、細胞集塊取出しの際に便利である
。図では一方に傾斜させたものが示されているが、漏斗
状にして中央部から細胞集塊を取出すようにしてもよい
。培養が終了し、ガスの供給をストップすると、浮遊し
ていた集塊は沈降し、第2図のようにそれぞれの大きさ
のメツシュにより各大きさのサイズに分かれる。ここで
バルブ38を開(と培養液は流れ出し、その流れととも
に2−以上の集塊25も排出される(第3図)0次にバ
ルブ40を開くと、同様に培養液とともに1〜2鴫の細
胞集塊27が排出される。このサイズの集塊が目的とす
るサイズであるから、そのまま2段目の培養槽に移され
る。同様にバルブ42を開け、■ffll11以下の集
塊29を取出す。また1IIII!1以下の集塊29は
さらに培養を続けると、集塊のサイズが1〜2mmにな
る可能性があるため、排出せず次の培養に用いてもよい
、この場合、コンディショニング培養となるため、次の
培養をさらにスムーズに行うことができる0例えば1段
目の培養において、2ffiI11以上の集塊と2mm
以下の集塊に分けることを目的とするとき、第4図に示
すように2mmのメツシュ41を培養槽に取付け、中央
部に設けた循環パイプ45と連絡管43を通して培養液
を循環させることによって撹拌してもよい。培養終了後
の操作は実施例1と同様にして行われる。図中40は培
養槽、47.49は取出し管、51は液の流線である。The apparatus shown in FIG. 1 includes a culture tank 20, a culture solution supply pipe 39 provided at the top thereof, and a culture solution supply pipe 39 provided at intervals in sequence in the culture solution flow path (in the vertical direction) in the culture tank 20. The first
Removal of cell aggregates provided at cell aggregate storage locations on the sieve 21 and the second sieve 23, the gas blowing pipe 31 inserted into the bottom of the culture tank, and the first sieve 21 and the second sieve 23. It consists of tubes 35, 37 and a similar extraction tube 33 provided at the bottom of the culture tank. In FIG. 1, for example, when the purpose is to obtain cell aggregates with a size of 1 to 2 mm in the first stage of culture, the first sieve 21 is a mesh of 2 filters, and the second sieve 23 is a mesh of 1 mo+. It is attached to the culture tank 20, and gas (air,
Supply oxygen, nitrogen, etc.) and stir. As the culture continues, most of the cell aggregates 25 that have grown to 2 mm or more are on the first sieve 21 in the culture tank, and the cell aggregates 25 that are 1 mm or less are
Most of 9 collects at the bottom of the culture tank, and the target 1
A ~2 m agglomerate 27 collects on the second sieve 23 in the middle of the culture tank. The material of the sieve (hereinafter also referred to as mesh) may be any durable material such as nylon or stainless steel, but it is preferably one that is resistant to heat in order to sterilize the culture tank. Furthermore, there are no particular restrictions on the size of the mesh or the location of its attachment; however, the smaller the volume of the target size portion, the better the efficiency of agglomerate classification. It is more convenient to attach the mesh at an angle as shown in the figure when removing cell clusters. Although the figure shows one tilted to one side, it may also be shaped like a funnel to take out the cell aggregate from the center. When the culture is completed and the gas supply is stopped, the floating agglomerates settle and are separated into different sizes by meshes of different sizes as shown in FIG. Here, the valve 38 is opened (and the culture solution flows out, and along with the flow, 2 or more aggregates 25 are also discharged (Fig. 3)).Next, when the valve 40 is opened, 1 to 2 aggregates 25 are also discharged along with the culture solution. Cell clusters 27 of size 11 and below are discharged.Since the clusters of this size are the target size, they are transferred as they are to the second stage culture tank.Similarly, open the valve 42 and collect the clusters 29 of 11 and below. In addition, if the agglomerate 29 with 1III!1 or less is further cultured, the size of the agglomerate may become 1 to 2 mm, so it may be used for the next culture without being discharged.In this case, the conditioner For example, in the first stage of culture, agglomerates of 2ffiI11 or more and 2mm
When the purpose is to divide into the following agglomerates, as shown in FIG. May be stirred. The operations after completion of the culture are carried out in the same manner as in Example 1. In the figure, 40 is a culture tank, 47, 49 is a take-out tube, and 51 is a liquid streamline.
[発明の効果〕
本発明によれば、細胞集塊サイズのための分級器を用い
ることなく、培養槽内で増殖とともに細胞集塊サイズに
よる分級を行うことができる。[Effects of the Invention] According to the present invention, it is possible to perform cell aggregation size classification as well as proliferation in a culture tank without using a classifier for cell agglomerate size.
第1図、第2図、第3図および第4図は、それぞれ本発
明の植物細胞培養装置を示す説明図、第5図および第6
図は、従来の植物細胞培養装置を示す説明図である。
20・・・培養槽、21・・・第1メツシユ、23.・
・第2メツシユ、25・・・第1の細胞集塊(大)、2
7・・・第2の細胞集塊(中)、29・・・第3の細胞
集塊(小)、31・・・ガス吹込み管、33.35.3
7・・・細胞集塊取出し管、L・・・液レベル。Figures 1, 2, 3 and 4 are explanatory diagrams showing the plant cell culture apparatus of the present invention, Figures 5 and 6, respectively.
The figure is an explanatory diagram showing a conventional plant cell culture device. 20... Culture tank, 21... First mesh, 23.・
・Second mesh, 25...first cell cluster (large), 2
7... Second cell aggregate (medium), 29... Third cell aggregate (small), 31... Gas blowing tube, 33.35.3
7...Cell cluster removal tube, L...Liquid level.
Claims (1)
と、該培養槽内の培養液の流路を遮るように設けられた
1以上のふるいと、該ふるいによって分級された細胞集
塊を槽外にそれぞれ取り出す手段とを有することを特徴
とする植物細胞培養装置。(1) A culture tank, a means for circulating a culture solution in the culture tank, one or more sieves provided to block the flow path of the culture solution in the culture tank, and cells classified by the sieve. 1. A plant cell culturing device characterized by having means for taking out each aggregate out of the tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1099701A JPH0661259B2 (en) | 1989-04-19 | 1989-04-19 | Plant cell culture equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1099701A JPH0661259B2 (en) | 1989-04-19 | 1989-04-19 | Plant cell culture equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02276566A true JPH02276566A (en) | 1990-11-13 |
JPH0661259B2 JPH0661259B2 (en) | 1994-08-17 |
Family
ID=14254361
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1099701A Expired - Lifetime JPH0661259B2 (en) | 1989-04-19 | 1989-04-19 | Plant cell culture equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0661259B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0365129A (en) * | 1989-08-01 | 1991-03-20 | Mitsui Petrochem Ind Ltd | Culture system |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63240773A (en) * | 1987-03-27 | 1988-10-06 | Komatsu Ltd | Bedding device |
-
1989
- 1989-04-19 JP JP1099701A patent/JPH0661259B2/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63240773A (en) * | 1987-03-27 | 1988-10-06 | Komatsu Ltd | Bedding device |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0365129A (en) * | 1989-08-01 | 1991-03-20 | Mitsui Petrochem Ind Ltd | Culture system |
Also Published As
Publication number | Publication date |
---|---|
JPH0661259B2 (en) | 1994-08-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Vogel et al. | Fermentation and biochemical engineering handbook: principles, process design and equipment | |
JPH09500818A (en) | Particle sedimentation tank used for cell culture | |
US20020155595A1 (en) | Intermittent immersion vessel apparatus and process for plant propagation | |
JPH07506250A (en) | Variable volume reactor type apparatus and method for culturing cellular material | |
JP6737813B2 (en) | Small-scale culture of suspension cells | |
Lian et al. | Bulblet formation from bulbscale segments of Lilium using bioreactor system | |
Conger et al. | Somatic embryo ontogeny in suspension cultures of orchardgrass | |
JPH02276566A (en) | Apparatus for culturing plant cell | |
Engvild | Plantlet ploidy and flower‐bud size in tobacco anther cultures | |
WO1991006627A1 (en) | Nested-cone separator | |
WO2021181784A1 (en) | Cell recovery device, cell recovery method, cell separation system, and cell separation method | |
CN210675560U (en) | Crystal and powder co-production device | |
JPH06209761A (en) | Cell culture system | |
CN210647289U (en) | Special flour production facility of high school low protein | |
CN2640593Y (en) | Sediment crystallizing reactor | |
SE537412C2 (en) | Process for removing liquid from a porous substrate in somatic plant embryogenesis | |
CN107234749A (en) | One kind is used for waste plastic bottle apparatus for crushing and treating | |
CN210279852U (en) | Chinese date proportion grading plant | |
CN213916107U (en) | Equipment for producing zinc material by atomization method | |
JPS609482A (en) | Highly-concentrated cultivation of floating cell and its device | |
CN211005428U (en) | Closed cell enlarging culture device | |
JPS5921388A (en) | Method for cell culture | |
CN220092102U (en) | Impurity screening plant is used in production of seasoning powder | |
CN111842122A (en) | Iron ore divides sieve device | |
CN220724161U (en) | Cell separation sieving mechanism |