JPS63109772A - Culture of vegetable cell or the like - Google Patents

Culture of vegetable cell or the like

Info

Publication number
JPS63109772A
JPS63109772A JP61257997A JP25799786A JPS63109772A JP S63109772 A JPS63109772 A JP S63109772A JP 61257997 A JP61257997 A JP 61257997A JP 25799786 A JP25799786 A JP 25799786A JP S63109772 A JPS63109772 A JP S63109772A
Authority
JP
Japan
Prior art keywords
culture
tank
plant cells
preculture
main
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
Application number
JP61257997A
Other languages
Japanese (ja)
Other versions
JPH0421472B2 (en
Inventor
Shozo Inoue
昌三 井上
Shuji Iwai
岩井 修司
Yoshinori Miyamoto
宮本 芳則
Toshiji Oba
利治 大場
Noriaki Chiba
千葉 則昭
Toshiyuki Kikuchi
菊地 敏行
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nitto Denko Corp
Original Assignee
Nitto Electric Industrial Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nitto Electric Industrial Co Ltd filed Critical Nitto Electric Industrial Co Ltd
Priority to JP61257997A priority Critical patent/JPS63109772A/en
Publication of JPS63109772A publication Critical patent/JPS63109772A/en
Publication of JPH0421472B2 publication Critical patent/JPH0421472B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

PURPOSE:To enable the production of vegetable cell in high yield, to remarkably improve its production efficiency and to simplify the operation, by culturing vegetable cell by a particular method using a preculture tank and a main culture tank. CONSTITUTION:Vegetable cells, etc., are precultured in a preculture tank 11 and then cultured in a main culture tank 12 until the concentration of the cell reaches a prescribed level. The cultured liquid is diluted with a fresh medium and a part of the diluted cultured liquid is supplied to the preculture tank 11 via a circulation path 14. The cultured liquid is again cultured in the preculture tank 11 until the vegetable cell concentration reaches a prescribed level and taken out of the tank through the delivery port 16.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、植物の細胞や組織を大量に効率よく培養する
方法に関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for efficiently culturing a large amount of plant cells and tissues.

(従来の技術) 植物の細胞や組織から、医薬などの有用な物質が得られ
ることがあり、このような有用な物質を恒常的に得るべ
く、植物の細胞や組織を工業的に培養することが試みら
れている。植物の細胞等は培養槽内で液内培養すること
が、大量培養し得るため、工業的には好適である。この
ため、従来は。
(Prior art) Useful substances such as medicines can be obtained from plant cells and tissues, and in order to permanently obtain such useful substances, it is necessary to industrially cultivate plant cells and tissues. is being attempted. Submerged culture of plant cells and the like in a culture tank is industrially preferred because it allows for mass culture. For this reason, traditionally.

培養槽を大型化することにより、大量に培養するという
方法が試みられていた。しかし、培養槽の大型化に伴い
、植物細胞は水頭圧や重力等により物理化学的な損傷を
受けやすくなると共に、培養条件の制御(二酸化炭素濃
度、 pit値、細胞の攪拌速度等の制御)が困難にな
る。という欠点を生じるものであった。このため、培養
槽を大型化することによる培養効率の向上が図れなかっ
た。
Attempts have been made to culture in large quantities by increasing the size of the culture tank. However, as culture tanks become larger, plant cells become more susceptible to physicochemical damage due to water head pressure, gravity, etc., and control of culture conditions (control of carbon dioxide concentration, pit value, cell agitation speed, etc.) becomes necessary. becomes difficult. This resulted in the following drawbacks. For this reason, it has not been possible to improve culture efficiency by increasing the size of the culture tank.

そこで、一定の条件化で連続的に培養する連続培養を用
い、細胞の培養速度を向上させる方法が試みられている
。理論的には、連続培養による培養が最も生産効率に優
れているが、植物細胞を無菌的にかつ連続的に収穫する
ことが技術的に困難である、しかも、連続培養を行うた
めの装置は。
Therefore, attempts have been made to improve the cell culture speed by using continuous culture, in which cells are continuously cultured under certain conditions. Theoretically, continuous culture has the highest production efficiency, but it is technically difficult to harvest plant cells continuously and aseptically, and the equipment for continuous culture is not available. .

その連続培養に最も適した条件にて設計、製作しなけれ
ばならず、また運転条件の決定も非常に困難であり、連
続培養を用いて、植物細胞等を工業的に培養することは
、実用化されていないのが現状である。
It must be designed and manufactured under the most suitable conditions for continuous culture, and it is also extremely difficult to determine the operating conditions, making it difficult to commercially cultivate plant cells using continuous culture. The current situation is that it has not been standardized.

一方、連続培養に対し、植物の細胞等を一定量の培地内
にて培養する回分培養も行われている。
On the other hand, in contrast to continuous culture, batch culture, in which plant cells and the like are cultured in a fixed amount of medium, is also performed.

第4図に、従来の回分培養装置の一例を示す。この図に
基づいて回分培養を説明すると、まず、植物細胞等を、
フラスコ51にて振とう培養する0次に、調整・細菌さ
れた培地を仕込んだ前培養槽52に振とう培養された植
物細胞を移植し、植物細胞を増殖させる。他方、前培養
槽52による前培養と平行して、主培養槽53では主培
養に備えて、培地の調整・細菌、および前培養槽52か
ら主培養槽53に連通ずる移送管54の殺菌を行う。主
培養槽53が大容量の場合には、培地膜面は連続殺菌装
置によって別に行い、その培地は、殺菌された主培養槽
へ連続的に仕込まれる。
FIG. 4 shows an example of a conventional batch culture device. To explain batch culture based on this diagram, first, plant cells etc.
Next, the shake-cultured plant cells are transplanted into a pre-culture tank 52 containing an adjusted and bacterium cultured medium, and the plant cells are multiplied. On the other hand, in parallel with the preculture in the preculture tank 52, in preparation for the main culture, the main culture tank 53 adjusts the culture medium, removes bacteria, and sterilizes the transfer pipe 54 communicating from the preculture tank 52 to the main culture tank 53. conduct. When the main culture tank 53 has a large capacity, the culture medium membrane surface is separately sterilized using a continuous sterilizer, and the culture medium is continuously fed into the sterilized main culture tank.

次いで、雑菌汚染を防ぐために、主培養槽53を通気加
圧しつつ培養温度に冷却後、前培養槽52から前培養し
た植物細胞を、移送管54にて主培養槽53へ移植し、
該主培養槽53内にて主培養が行われる。主培養槽53
による培養中は、該主培養53内の温度・ptiを設定
値に制御し、好気培養の場合には攪拌翼53aにより攪
拌を行うと共に、空気供給管55より送給される無菌空
気にて通気する。そして。
Next, in order to prevent bacterial contamination, the main culture tank 53 is cooled to culture temperature while being ventilated and pressurized, and the precultured plant cells are transferred from the pre-culture tank 52 to the main culture tank 53 via a transfer pipe 54.
Main culture is performed in the main culture tank 53. Main culture tank 53
During the culture, the temperature and PTI in the main culture 53 are controlled to the set values, and in the case of aerobic culture, stirring is performed using the stirring blades 53a, and sterile air is supplied from the air supply pipe 55. Ventilate. and.

このような主培養により、植物細胞が所定濃度に達した
時点で培養は終了する。培養終了後、所定濃度の植物細
胞を含む培養液は、主培養槽53の収穫口53bから生
産物回収工程へと移され、主培養槽53は2次の培養の
ために、洗浄・殺菌が行われる。以上の工程で、保存植
物細胞から出発して。
With this main culture, the culture is terminated when the plant cells reach a predetermined concentration. After culturing, the culture solution containing a predetermined concentration of plant cells is transferred to the product recovery process from the harvest port 53b of the main culture tank 53, and the main culture tank 53 is washed and sterilized for secondary culture. It will be done. The above steps start from preserved plant cells.

大量培養による植物細胞の生産が行われる。Plant cells are produced by mass culture.

このような主培養槽53を中心にした回分培養では、培
養槽の準備時間(洗浄・培地調整・殺菌・冷却等に要す
る時間)、培養時間(接種時間も含む)、培養液の排出
時間の和が、1回の回分培養に要する時間となる。
In batch culture centered on the main culture tank 53, the preparation time of the culture tank (time required for cleaning, medium adjustment, sterilization, cooling, etc.), culture time (including inoculation time), and culture solution drain time are The sum is the time required for one batch culture.

このように2回分培養では、主培養槽53による生産段
階の前に、数段の“種(seed)  ”培養段階の前
培養が必要である。主培養は前培養の約10倍の規模と
なるため、前培養の過程を多段階にしなければならず、
また前培養槽52自体の容量も大きくしなければならな
い。従って2回分培養では。
Thus, in the double culture, several "seed" culture stages are required before the production stage in the main culture tank 53. Since the main culture is approximately 10 times larger than the preculture, the preculture process must be performed in multiple stages.
Furthermore, the capacity of the preculture tank 52 itself must be increased. Therefore, in double culture.

設備効率が悪く、また大量生産ができないために。This is because equipment efficiency is poor and mass production is not possible.

工業的には不向きである。回分培養では1種培養段階で
ある前培養を不要にした反復回分培養もあるが、このよ
うな反復回分培養も生産効率が悪く。
It is not suitable for industrial use. In batch culture, there is also a repetitive batch culture that eliminates the need for preculture, which is a single culture stage, but such repetitive batch culture also has poor production efficiency.

収N量そのものは増大しない。The N yield itself does not increase.

(発明が解決しようとする問題点) 本発明は上記従来の問題を解決するものであり。(Problem to be solved by the invention) The present invention solves the above-mentioned conventional problems.

その目的は、前培養を行う前培養槽と主培養を行う主培
養槽とを用いて、植物細胞等の生産効率を著しく向上さ
せることができる培養方法を提供することにある。
The purpose is to provide a culture method that can significantly improve the production efficiency of plant cells, etc. by using a preculture tank for preculture and a main culture tank for main culture.

(問題点を解決するための手段) 本発明の植物細胞等の培養方法は、主培養を行う主培養
槽と、該主培養槽の前段にて前培養を行う前培養槽とに
より、植物の細胞や組織等を培養する方法であり、主培
養槽にて植物細胞等を所定濃度にまで培養する工程と、
植物細胞等が所定濃度にまで培養された該培養液を培地
にて希釈する工程と、希釈された該培養液の一部を前培
養槽にて植物細胞等が所定濃度になるまで培養する工程
と、植物細胞が所定濃度にまで培養された前培養槽内の
該培養液を取り出す工程と、を包含し、そのことにより
上記目的が達成される。
(Means for Solving the Problems) The method for cultivating plant cells, etc. of the present invention uses a main culture tank for main culture and a pre-culture tank for pre-culture at the stage before the main culture tank. It is a method of culturing cells, tissues, etc., which includes the step of culturing plant cells, etc. to a predetermined concentration in a main culture tank,
A step of diluting the culture solution in which plant cells, etc. have been cultured to a predetermined concentration with a medium, and a step of culturing a part of the diluted culture solution in a pre-culture tank until the plant cells, etc. reach a predetermined concentration. and a step of taking out the culture solution in the preculture tank in which the plant cells have been cultured to a predetermined concentration, thereby achieving the above object.

(実施例) 以下に本発明を実施例について説明する。(Example) The present invention will be described below with reference to Examples.

本発明の培養方法は9例えば第1図に示すように、前培
養を行う前培養槽11と、主培養を行う主培養槽12と
により、植物の細胞や組織の培養が行われる。前培養槽
11の下部は主培養槽12の上部に。
In the culture method of the present invention, for example, as shown in FIG. 1, plant cells and tissues are cultured in a preculture tank 11 that performs preculture and a main culture tank 12 that performs main culture. The lower part of the pre-culture tank 11 is the upper part of the main culture tank 12.

移送管13を介して連通している。また、該前培養槽1
1の下部は収穫口16にも連通している。主培養槽12
の下部は、循環路14を介して前培養槽11の上部に連
通している。前培養槽11の下部および主培養槽12の
下部には、無菌空気の供給管15の排出口がそれぞれ配
設されている。前培養槽11内および主培養槽12内に
は、それぞれ攪拌翼11aおよび12aが配設されてい
る。
They communicate via a transfer pipe 13. In addition, the pre-culture tank 1
The lower part of 1 also communicates with the harvesting port 16. Main culture tank 12
The lower part thereof is in communication with the upper part of the pre-culture tank 11 via the circulation path 14. At the lower part of the pre-culture tank 11 and the lower part of the main culture tank 12, discharge ports of sterile air supply pipes 15 are provided, respectively. Stirring blades 11a and 12a are provided in the preculture tank 11 and the main culture tank 12, respectively.

このような培養装置による本発明方法を説明すると、ま
ず、植物細胞をフラスコ17内にて振とう培養し増殖さ
せる。次に、!j1整・殺菌された培地を前培養槽11
に仕込んでおき、該前培養槽11内の培地内へ、振とう
培養により増殖された植物細胞を移植する。そして、該
前培養槽11にて植物細胞を前培養する。
To explain the method of the present invention using such a culturing device, first, plant cells are cultured in a flask 17 with shaking and propagated. next,! j1 Prepared and sterilized medium is transferred to preculture tank 11
The plant cells grown by shaking culture are transplanted into the medium in the preculture tank 11. Then, plant cells are precultured in the preculture tank 11.

この前培養の間に、主培養槽12内での主培養に備えて
、培地の調整・殺菌および移送管13の殺菌を行う。主
培養槽12が大容量の場合には、培地殺菌は培地調整槽
あるいは連続培地殺菌装置によって別に行われ、殺菌さ
れた培地が主培養槽12へ連続的に仕込まれる。
During this pre-culture, the culture medium is adjusted and sterilized and the transfer tube 13 is sterilized in preparation for the main culture in the main culture tank 12. When the main culture tank 12 has a large capacity, culture medium sterilization is performed separately by a culture medium adjustment tank or a continuous culture medium sterilizer, and the sterilized culture medium is continuously charged into the main culture tank 12.

次いで雑菌汚染を防止するために、主培養槽12を、供
給管15からの無菌空気により通気加圧しつつ培養温度
に冷却後、前培養槽11にて前培養した植物細胞を、移
送管13から主培養槽12内へ移植して、主培養が開始
される。
Next, in order to prevent bacterial contamination, the main culture tank 12 is cooled to culture temperature while being ventilated and pressurized with sterile air from the supply pipe 15 , and then the plant cells precultured in the pre-culture tank 11 are transferred from the transfer pipe 13 . After transplanting into the main culture tank 12, main culture is started.

主培養槽12内での主培養中は、温度・pHを設定値に
制御し、また、好気培養の場合には供給管15から主培
養槽12内へ無菌空気を通気しつつ攪拌翼12aにて攪
拌する。植物細胞が所定濃度に達すると、主培養は終了
する。
During the main culture in the main culture tank 12, the temperature and pH are controlled to set values, and in the case of aerobic culture, sterile air is aerated into the main culture tank 12 from the supply pipe 15 while stirring blades 12a Stir at . When a predetermined concentration of plant cells is reached, the main culture is terminated.

主培養槽12内における主培養が終了した時点で。At the time when the main culture in the main culture tank 12 is completed.

前培養槽11内で培地を調整・殺菌し、該培地を加圧し
た状態で移送管13から主培養槽12へ送給する。
The culture medium is adjusted and sterilized in the preculture tank 11, and the medium is fed under pressure to the main culture tank 12 from the transfer pipe 13.

培地調整槽あるいは連続培地殺菌装置が配設される場合
には、新鮮培地を必要量だけ主培養槽12内へ送給する
When a culture medium adjustment tank or a continuous culture medium sterilization device is provided, the required amount of fresh culture medium is fed into the main culture tank 12.

主培養槽12内へ送給された培地は、所定濃度の植物細
胞を有する培養液と共に攪拌・混合されて。
The medium fed into the main culture tank 12 is stirred and mixed with a culture solution containing a predetermined concentration of plant cells.

該培養液は希釈される。主培養槽12内で、培養液は十
分に攪拌されて、植物細胞が均一に分散される。次いで
、主培養槽12の内圧は、供給管15から送給される無
菌空気にて、前培養槽11の内圧と培養液圧との和以上
の圧力とされ、希釈された培養液は、殺菌された循環路
14を通って、前培養槽11内へ送給される。これによ
り、前培養槽11内および主培養槽12内には、植物細
胞の濃度、培地成分等が等しい培養液が仕込まれた状態
となる。
The culture solution is diluted. In the main culture tank 12, the culture solution is sufficiently stirred to uniformly disperse the plant cells. Next, the internal pressure of the main culture tank 12 is made equal to or higher than the sum of the internal pressure of the pre-culture tank 11 and the culture solution pressure using sterile air supplied from the supply pipe 15, and the diluted culture solution is sterilized. It is fed into the preculture tank 11 through the circulation path 14 . As a result, the preculture tank 11 and the main culture tank 12 are filled with culture solutions having the same concentration of plant cells, medium components, and the like.

前培養槽11内に送給された培養液は、植物細胞が所定
濃度になるまで培養され、植物細胞が所定濃度になると
前培養槽11内の培養は終了する。そして、該前培養槽
11内の培養液は収穫口16より収穫される。主培養槽
12内では、前培養槽11内にて培養が行われている間
も培養が行われる。
The culture solution fed into the preculture tank 11 is cultured until the plant cells reach a predetermined concentration, and when the plant cells reach a predetermined concentration, the culture in the preculture tank 11 ends. The culture solution in the pre-culture tank 11 is harvested from the harvest port 16. Culture is carried out in the main culture tank 12 even while culture is being carried out in the pre-culture tank 11.

培養液が収穫された前培養槽11内では、引き続き、培
地を調整・殺菌し、その培地は移送管14から主培養槽
12内へ送給される。この場合、前述のように、培地調
整槽あるいは連続培地殺菌装置が配設されていれば、培
地調整槽あるいは連続培地殺菌装置から新鮮培地が主培
養槽12内へ送給される。そして、前培養槽11におけ
る培養の間に、主培養槽12内にて植物細胞が培養され
た培養液は。
In the pre-culture tank 11 from which the culture solution has been harvested, the medium is subsequently adjusted and sterilized, and the medium is fed into the main culture tank 12 from the transfer pipe 14. In this case, as described above, if a culture medium adjustment tank or continuous culture medium sterilizer is provided, fresh culture medium is fed into the main culture tank 12 from the culture medium adjustment tank or continuous culture medium sterilizer. The culture solution in which the plant cells were cultured in the main culture tank 12 during the culture in the pre-culture tank 11 is.

送給される培地により希釈される。It is diluted by the medium being delivered.

以後、前述したように、希釈された培養液の一部が前培
養槽11へ送給されて培養され、植物細胞が所定濃度に
なれば収穫口16から収穫される。
Thereafter, as described above, a portion of the diluted culture solution is fed to the preculture tank 11 and cultured, and when the plant cells reach a predetermined concentration, they are harvested from the harvest port 16.

第2図は1本発明方法の実施に使用する装置の別の実施
例を示す模式図である。この実施例では。
FIG. 2 is a schematic diagram showing another embodiment of the apparatus used to carry out the method of the present invention. In this example.

主培養槽12における主培養の前段階である前培養を、
2つの前培養槽11および11′で行うようになってい
る。このような装置では、主培養槽12にて植物細胞が
所定濃度にまで培養された培養液を。
The preculture, which is a stage before the main culture in the main culture tank 12,
The process is carried out in two preculture tanks 11 and 11'. In such an apparatus, a culture solution in which plant cells are cultured to a predetermined concentration in a main culture tank 12 is used.

培地で希釈して、各前培養槽11および11″で再び植
物細胞が所定濃度になるまで培養し、各前培養槽11お
よび11°の収穫口16および16゛から植物細胞が収
穫される。
After diluting with a medium, the plant cells are again cultured in each pre-culture tank 11 and 11'' until a predetermined concentration is reached, and the plant cells are harvested from the harvest ports 16 and 16' in each pre-culture tank 11 and 11°.

植物の細胞等は、′R1生物とは異なり2体外(培地)
に生長限外物を作らないために2本発明方法のように、
新鮮培地と酸素、さらには適当な空間を与えれば効率よ
く生長する。
Unlike 'R1 organisms, plant cells etc. are grown outside the body (medium).
In order to avoid producing growth substances, as in the method of the present invention,
If given fresh medium, oxygen, and adequate space, they will grow efficiently.

本発明方法による生産量と、従来の回分培養による生産
量とを簡単なモデルにより比較する。今。
The production amount by the method of the present invention and the production amount by conventional batch culture will be compared using a simple model. now.

30日間の回分培養で、濃度(WET )が3%から3
0%に生長する植物細胞を考える。通常、誘導期間とし
て3〜5日程度考えられるが、比増殖速度(μ)が一定
であり、常に対数増殖するとすれば。
In batch culture for 30 days, the concentration (WET) was 3% to 3.
Consider a plant cell growing at 0%. Usually, the induction period is considered to be about 3 to 5 days, assuming that the specific growth rate (μ) is constant and the growth is always logarithmic.

比増殖速度(μ)は2通常、(l)式で表される。The specific growth rate (μ) is usually expressed by the formula (l).

ただし Δt:時間(日数) χo:カルスの初期濃度 X :Δを後のカルス濃度 上記モデルをこの(11式に当てはめると、比増殖速度
μは。
Where, Δt: Time (days) χo: Initial concentration of callus

・・・・(1)。...(1).

となる。becomes.

1年間の収穫量Yは。What is the annual harvest Y?

Y−(収穫時のカルス濃度(%)〕 ・ 〔主培養容量
(1)〕 ・ 〔11年の培養回数〕・ ・ ・ ・(
2) で表されるので、主培養槽の容量を1001とすると、
従来の回分培養による1年間の収1量Yは。
Y- (Callus concentration at harvest (%)) ・ [Main culture capacity (1)] ・ [Number of culture in 11 years] ・ ・ ・ ・ (
2) Therefore, if the capacity of the main culture tank is 1001,
What is the annual yield Y of conventional batch culture?

=  360 (kg/year)       ・・
・・(2)’(ただし主培養槽の洗浄時間は含まれない
)となる。
= 360 (kg/year)...
...(2)' (However, the cleaning time of the main culture tank is not included).

このような植物細胞を本発明方法により培養した場合を
考える。ただし1本発明方法では、濃度が30%に増殖
した植物細胞を、−旦、27%まで培地により希釈し、
その後に前培養槽にて30%まで増殖させて収穫するも
のとする。 (1)’ 式より、該植物細胞の比増殖速
度μが0.0767 (day”)であることから、植
物細胞が27%から30%までに増殖する時間Δtは、
(1)式より となる。収穫時のロスタイムを考慮して、1.5(da
y)に1回収穫するものとすると、1年間の収穫量Yは
、(2)式から次のようになる。ただし1本発明方法に
よれば、植物細胞を3%から30%まで増殖し、その後
、−旦27%に希釈した後30%に増殖させるものであ
るため、3%から30%まで増殖する当初の30日間は
収穫されない。従って。
Consider the case where such plant cells are cultured by the method of the present invention. However, in the method of the present invention, plant cells grown to a concentration of 30% are diluted to 27% with a medium,
Thereafter, the seeds will be grown to 30% in a preculture tank and harvested. From the formula (1)', since the specific growth rate μ of the plant cell is 0.0767 (day"), the time Δt for the plant cell to grow from 27% to 30% is:
From equation (1). 1.5 (da) considering loss time during harvesting.
Assuming that the crop is harvested once in y), the annual harvest amount Y is calculated from equation (2) as follows. However, according to the method of the present invention, plant cells are grown from 3% to 30%, and then diluted to 27% and then grown to 30%. It will not be harvested for 30 days. Therefore.

+ao−690(kg/year) となる。+ao-690 (kg/year) becomes.

このように3本発明方法によれば、1年間に植物細胞が
従来の回分培養の約2倍収穫することができる。
As described above, according to the method of the present invention, approximately twice as many plant cells can be harvested in one year as compared with conventional batch culture.

(実験例) 第1図に示す装置を用い、容fix、1ozO前培養槽
に、8(H!の培地を仕込み、また、容16oozの主
培養槽に4001の培地を仕込んで、オタネニンジンを
通気・攪拌培養した。培地としてはB5培地を使用し、
培養温度を25℃9通気空気量を0.1〜0.4VVM
とした。当初の1か月間は収穫できないが、1か月経過
後7日ごとに前培養槽から植物細胞を収穫した。従来の
回分培養では、28日間の培養で80kg (WET 
)の細胞が得られ、6か月では480 kgの細胞が得
られるが1本発明方法では、6か月間に770kg (
従来より60%増)の植物細胞が得られた。第3図にそ
の結果を示す。
(Experiment example) Using the apparatus shown in Figure 1, a medium of 8 (H!) was placed in a pre-culture tank with a fixity of 1 oz, and a medium of 4001 was placed in a main culture tank of 16 oz.・Agitation culture was carried out.B5 medium was used as the medium,
Culture temperature: 25℃9 Aeration air volume: 0.1-0.4VVM
And so. Plant cells could not be harvested during the first month, but after one month, plant cells were harvested from the preculture tank every 7 days. In conventional batch culture, 80 kg (WET
), and 480 kg of cells can be obtained in 6 months; however, with the method of the present invention, 770 kg (
60% more plant cells than before were obtained. Figure 3 shows the results.

(発明の効果) 本発明方法は、このように、主培養槽内の植物細胞等の
濃度を、常に、収穫時の所定濃度付近の高濃度に維持で
き、容量の小さい前培養槽内にて所定濃度にまで培養し
て収穫するものであるから。
(Effects of the Invention) As described above, the method of the present invention can always maintain the concentration of plant cells, etc. in the main culture tank at a high concentration near the predetermined concentration at the time of harvest, and in the pre-culture tank with a small capacity. This is because it is harvested after culturing to a predetermined concentration.

植物細胞等を高効率に収穫できる。当初、前培養槽に種
培養された植物細胞を主培養槽に移植すれば、その後の
種培養は不要になり掻作が簡略化される。従来の回分培
養の装置に対して、無菌フィルタを用いて循環路を配設
すればよく、従って。
Plant cells etc. can be harvested with high efficiency. Initially, if the plant cells seed-cultured in the pre-culture tank are transplanted to the main culture tank, subsequent seed culture is unnecessary and the scraping process is simplified. For conventional batch culture apparatuses, a circulation path may be provided using a sterile filter.

既設設備を利用して収穫量を増大させることができる。Yields can be increased using existing equipment.

4、 パ  の  ゛なU 第1図は本発明方法の実施に使用する装置の一例を示す
模式図、第2図はその別の例を示す模式図、第3図は本
発明方法による収Pi量を示すグラフ、第4図は従来の
回分培養装置の一例を示す模式図である。
4. U of P Figure 1 is a schematic diagram showing an example of the apparatus used to carry out the method of the present invention, Figure 2 is a schematic diagram showing another example thereof, and Figure 3 is a schematic diagram showing an example of the apparatus used to carry out the method of the present invention. The graph showing the amount, FIG. 4, is a schematic diagram showing an example of a conventional batch culture device.

11、11’ ・・・前培養槽、12・・・主培養槽、
13・・・移送管、14・・・循環路、15・・・供給
管、 16.16’ ・・・収穫口。
11, 11'... Preculture tank, 12... Main culture tank,
13... Transfer pipe, 14... Circulation path, 15... Supply pipe, 16.16'... Harvesting port.

以上that's all

Claims (1)

【特許請求の範囲】 1、主培養を行う主培養槽と、該主培養槽の前段にて前
培養を行う前培養槽とにより、植物の細胞や組織等を培
養する方法であり、 主培養槽にて植物細胞等を所定濃度にまで培養する工程
と、 植物細胞等が所定濃度にまで培養された該培養液を培地
にて希釈する工程と、 希釈された該培養液の一部を前培養槽にて植物細胞等が
所定濃度になるまで培養する工程と、植物細胞が所定濃
度にまで培養された前培養槽内の該培養液を取り出す工
程と、 を包含する植物細胞等の培養方法。
[Scope of Claims] 1. A method for culturing plant cells, tissues, etc. using a main culture tank that performs main culture and a preculture tank that performs preculture before the main culture tank, A step of culturing plant cells etc. to a predetermined concentration in a tank, a step of diluting the culture solution in which the plant cells etc. have been cultured to a predetermined concentration with a medium, and a step of diluting a part of the diluted culture solution beforehand. A method for culturing plant cells, etc., comprising: culturing the plant cells, etc. in a culture tank until they reach a predetermined concentration; and removing the culture solution in the preculture tank in which the plant cells have been cultured to the predetermined concentration. .
JP61257997A 1986-10-28 1986-10-28 Culture of vegetable cell or the like Granted JPS63109772A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61257997A JPS63109772A (en) 1986-10-28 1986-10-28 Culture of vegetable cell or the like

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61257997A JPS63109772A (en) 1986-10-28 1986-10-28 Culture of vegetable cell or the like

Publications (2)

Publication Number Publication Date
JPS63109772A true JPS63109772A (en) 1988-05-14
JPH0421472B2 JPH0421472B2 (en) 1992-04-10

Family

ID=17314100

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61257997A Granted JPS63109772A (en) 1986-10-28 1986-10-28 Culture of vegetable cell or the like

Country Status (1)

Country Link
JP (1) JPS63109772A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010525833A (en) * 2007-05-07 2010-07-29 プロタリクス リミテッド Large-scale disposable bioreactor
US8449876B2 (en) 2003-04-27 2013-05-28 Protalix Ltd. Human lysosomal proteins from plant cell culture

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101098072B1 (en) 2008-03-10 2011-12-26 이비덴 가부시키가이샤 Flexible wiring board and method of manufacturing same

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8449876B2 (en) 2003-04-27 2013-05-28 Protalix Ltd. Human lysosomal proteins from plant cell culture
US8741620B2 (en) 2003-04-27 2014-06-03 Protalix Ltd. Human lysosomal proteins from plant cell culture
JP2010525833A (en) * 2007-05-07 2010-07-29 プロタリクス リミテッド Large-scale disposable bioreactor
US10364413B2 (en) 2007-05-07 2019-07-30 Protalix Ltd. Large scale disposable bioreactor

Also Published As

Publication number Publication date
JPH0421472B2 (en) 1992-04-10

Similar Documents

Publication Publication Date Title
CN102150624B (en) Tissue culture and rapid propagation method for pinellia tuber plant
CN102102081B (en) Pure-culture solid-state fermentation apparatus capable of gas-phase inoculation and feeding, and method thereof
CN107937329A (en) A kind of method for improving liquid spawn vigor
CN111528103B (en) Plant tissue culture reactor and amplification culture method thereof
CN111386963A (en) Tremella aurantialba cultivation method using tremella aurantialba seedling inoculation
JP2002051639A (en) Method for producing liquid spawn of mushroom and apparatus for inoculation of liquid spawn
JP2747972B2 (en) Complex large-scale culture of aerobic and anaerobic microorganisms
JPS63109772A (en) Culture of vegetable cell or the like
CN110679520A (en) Breeding method of lake culture strain
JPH10201467A (en) Judgement of growth of material to be cultured and culture apparatus therefor
JP2516106B2 (en) Tilapia farming method
JPH10113095A (en) Method for culturing water flea
CN114836462A (en) Efficient agrobacterium-mediated genetic transformation method for melons
WO2019157785A1 (en) Production process and equipment for continuously supplying bacterial liquid in exponential growth phase
CN107794224A (en) A kind of method for preserving of golden mushroom pompon
JPH02174674A (en) Method for culturing lactic acid bacterium and apparatus used therefor
JPH06292478A (en) Tissue culture of plant of family orchidaceae
JPH0662662A (en) Method for artificially culturing mushrooms
JPS5945879A (en) Method and apparatus for vapor-phase cultivation of vegetable tissue
JPH09201189A (en) Plant cell culture
SU878788A1 (en) Method of multistep culturing of baker yeast
SU566872A1 (en) Method of preparation of yeast for spiritus fermentation
JP2668107B2 (en) High-density mass-culture method for rotifers
JPH1084802A (en) Mass culture method for carrot adventious embryo
JPH0339021A (en) Continuous culture of rotifer