JPH0838157A - Culture solution conveyer - Google Patents
Culture solution conveyerInfo
- Publication number
- JPH0838157A JPH0838157A JP18220694A JP18220694A JPH0838157A JP H0838157 A JPH0838157 A JP H0838157A JP 18220694 A JP18220694 A JP 18220694A JP 18220694 A JP18220694 A JP 18220694A JP H0838157 A JPH0838157 A JP H0838157A
- Authority
- JP
- Japan
- Prior art keywords
- culture solution
- transfer
- pressure
- gas
- 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.)
- Pending
Links
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
Landscapes
- Wood Science & Technology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical & Material Sciences (AREA)
- Zoology (AREA)
- Biomedical Technology (AREA)
- Sustainable Development (AREA)
- Microbiology (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Biotechnology (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は培養液移送装置に関し、
さらに詳しくは培養液中の菌体を破損させることなく培
養液とともに連続的に移送することができる培養液移送
装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a culture medium transfer device,
More specifically, it relates to a culture medium transfer device capable of continuously transferring cells together with the culture medium without damaging the cells in the culture medium.
【0002】[0002]
【従来の技術】バイオ技術を利用した各種の菌体を用い
た培養工程において、培養槽で培養され、増殖した各種
菌体は、培養液とともにリサイクル移送やワンスルー移
送され、また培養終了後には分離工程への移送等が行わ
れる。従来、液体移送には、各種のポンプ、例えば渦巻
き式(遠心式)、タイヤフラム式、プランジャー式、ロ
ーラー式などのポンプが広く使用されている。しかしな
がら、培養された菌体を含む培養液の移送に上記ポンプ
を用いると、例えば、遠心式の場合には、回転羽根の高
速回転によりケーシングと羽根との間で剪断力が作用す
るため、培養された菌体が切断され、増殖が阻害される
という問題があった。このような問題は、特に植物細胞
や動物細胞、例えばスピルリナ、アナベナ等の糸状形態
のもの、数μm〜数10μmサイズのもの等に対して顕
著に発生する。また小型装置では、プランジャーポン
プ、ローラーポンプ、チューブポンプ等が使用されてい
るが、プランジャーポンプは脈動の発生により流量制御
が不安定であり、またローラーポンプやチューブポンプ
はローラーやチューブの消耗によるメンテナンスの手間
と費用の発生が伴うため十分とは言い難い。2. Description of the Related Art In a culturing process using various types of cells using biotechnology, various types of cells that have been cultivated in a culture tank and proliferated are recycled or one-through transferred together with a culture solution, and separated after the culturing is completed. Transfer to the process is performed. Conventionally, various types of pumps have been widely used for liquid transfer, for example, a spiral (centrifugal) type, a tire flam type, a plunger type, and a roller type pump. However, when the above-mentioned pump is used to transfer the culture solution containing the cultured cells, for example, in the case of a centrifugal type, a shearing force acts between the casing and the blade due to the high speed rotation of the rotating blade, so that the culture is performed. There was a problem that the microbial cells were cut and their growth was inhibited. Such a problem remarkably occurs particularly in plant cells and animal cells, for example, filamentous forms such as spirulina and anabaena, and those having a size of several μm to several tens of μm. In addition, plunger pumps, roller pumps, tube pumps, etc. are used in small devices, but the flow rate control of the plunger pump is unstable due to the occurrence of pulsation, and the roller pump and the tube pump consume the rollers and tubes. It is hard to say that it is sufficient because maintenance work and maintenance costs are required.
【0003】[0003]
【発明が解決しようとする課題】本発明の目的は、上記
従来技術の問題を解決し、培養液中の菌体を損傷するこ
となく培養液とともに連続的に移送することができる培
養液移送装置を提供することにある。The object of the present invention is to solve the above-mentioned problems of the prior art and to transfer a culture solution continuously with the culture solution without damaging the cells in the culture solution. To provide.
【0004】[0004]
【課題を解決するための手段】本願で特許請求される発
明は以下の通りである。 (1)培養槽内の菌体を含む培養液を一時的に貯溜す
る、並列に設けられた二以上の移送受タンクと、該各移
送受タンク内の培養液面を検出する液面センサーと、上
記培養槽から各移送受タンクに培養液を移送する移送配
管と、各移送受タンク内の培養液を排出する排出配管
と、各移送受タンク内に圧送ガスを導入する圧送ガス導
入配管、各移送受けタンク内のガスを排出するガス排出
配管および圧送ガスの圧力を検出する圧力センサーと、
上記各移送受タンクの移送配管、排出配管、圧送ガス導
入配管およびガス排出配管にそれぞれ設置された調節弁
と、上記各液面センサーおよび圧力センサーの信号に基
づき、各移送受タンクへの培養液の貯溜と各移送受タン
クからの培養液の排出を順次繰り返し行って培養液を連
続的に排出するように各調節弁の開閉および圧送ガスの
圧力を調節する制御装置とを備えたことを特徴とする培
養液移送装置。The inventions claimed in this application are as follows. (1) Two or more transfer receiving tanks arranged in parallel for temporarily storing a culture solution containing bacterial cells in a culture tank, and a liquid level sensor for detecting the culture solution level in each transfer receiving tank A transfer pipe for transferring the culture solution from the culture tank to each transfer receiving tank, a discharge pipe for discharging the culture solution in each transfer receiving tank, and a pressure-feeding gas introducing pipe for introducing a pressure-feeding gas into each transfer receiving tank, A gas discharge pipe for discharging the gas in each transfer receiving tank and a pressure sensor for detecting the pressure of the pressure-fed gas,
Based on the signals of the transfer pipes, discharge pipes, pressure-feeding gas introduction pipes and gas discharge pipes of the transfer receiving tanks and the liquid level sensors and pressure sensors, the culture solution to the transfer receiving tanks. And a control device that controls the opening and closing of each control valve and the pressure of the pressure-fed gas so that the culture solution is continuously discharged by sequentially and repeatedly storing the culture solution and discharging the culture solution from each transfer receiving tank. And a culture medium transfer device.
【0005】本発明において、移送受タンクは、連続的
に培養液を移送するため並列に二個以上、好ましくは3
〜4個設けられ、これらの移送受タンクに一時的に貯溜
された培養液の排出は、機械的な駆動駆動を用いずに加
圧ガスによる静圧下で行われる。すなわち、培養液が貯
溜されている一つのタンクに加圧したガスを圧送して培
養液を排出させ、かつ該一つのタンクから培養液を排出
している間に他のタンクに培養液を貯溜し、一つのタン
クの培養液の排出が終了した後、続いて他のタンクに圧
送ガスを供給し、培養液を連続して排出するようにされ
る。In the present invention, two or more transfer receiving tanks are arranged in parallel, preferably three, in order to transfer the culture solution continuously.
The discharge of the culture solution, which is provided in four units and temporarily stored in these transfer receiving tanks, is performed under static pressure by the pressurized gas without using mechanical drive. That is, the pressurized gas is sent under pressure to one tank in which the culture solution is stored to discharge the culture solution, and while the culture solution is discharged from the one tank, the culture solution is stored in another tank. Then, after the discharge of the culture solution from one tank is completed, the pumping gas is continuously supplied to the other tank to continuously discharge the culture solution.
【0006】各移送タンクの培養液の貯溜、排出および
圧送ガスの導入の切替えは、各移送受タンクに設けられ
たそれぞれの調節弁の開閉により行われ、その開閉の調
節は、各タンクの液面センサーの信号に基づき制御装置
により行われる。また圧送ガスの圧力は、通常、1〜1
0kg/cm2 Gとされるが、培養液の貯溜速度および
排出速度に応じて各移送受タンクの培養液の貯溜および
排出が順に繰り返して連続的に行われるように圧力セン
サーで検出された信号に基づいて制御装置により調節さ
れる。圧送ガスには、例えば、除湿、除菌処理等が施さ
れた空気、窒素ガス、CO2 ガス、燃焼排ガスなどの各
種ガスが用いられる。[0006] The storage and discharge of the culture solution in each transfer tank and the introduction of the pressure-fed gas are switched by opening and closing the respective control valves provided in each transfer receiving tank. It is performed by the controller based on the signal from the surface sensor. The pressure of the pressure-fed gas is usually 1 to 1
It is 0 kg / cm 2 G, but the signal detected by the pressure sensor is such that the storage and discharge of the culture solution in each transfer receiving tank are sequentially and continuously repeated according to the storage rate and the discharge rate of the culture solution. Is adjusted by the controller based on As the pressure-fed gas, various gases such as air, nitrogen gas, CO 2 gas, and combustion exhaust gas that have been dehumidified and sterilized are used.
【0007】以下に本発明の培養液移送装置を図面によ
り詳しく説明する。図1は、本発明の一実施例を示す培
養液移送装置の説明図である。図において、培養液移送
装置は、培養槽17内の菌体を含む培養液20を一時的
に貯溜する並列に設けられた第1移送受タンク1および
第2移送受タンク6と、該各タンク内の培養液面を検出
する液面センサー5、10と、上記培養槽17から各タ
ンク1、6に培養液を移送する移送配管11と、各タン
ク内の培養液を排出する排出配管13と、各タンク内に
圧送ガスを導入する圧送ガス導入配管12、各タンクな
いのガスを排出するガス排出配管24および圧送ガスの
圧力を検出する圧力センサー16と、上記移送配管11
に設けられた第1移送受タンクの移送調節弁2および第
2移送受タンクの移送調節弁7と、上記排出配管13に
設けられた第1移送受タンクの排出調節弁4および第2
移送受タンクの排出調節弁9と、圧送ガス導入配管12
に設けられた第1移送受タンクの圧送ガス調節弁3およ
び第2移送受タンクの圧送ガス調節弁8と、ガス排出配
管24に設けられた第1移送受タンクのガス排出調節弁
22および第2移送タンクのガス排出調節弁23と、上
記各液面センサー5、10および圧力センサー16の信
号に基づいて第1移送受タンクおよび第2移送受タンク
の各調節弁2、7、4、9、3、8、22、23の開閉
および圧送ガスの圧力を調節する制御装置15とから主
として構成される。The culture medium transfer device of the present invention will be described in detail below with reference to the drawings. FIG. 1 is an explanatory view of a culture medium transfer device showing an embodiment of the present invention. In the figure, the culture medium transfer device includes a first transfer receiving tank 1 and a second transfer receiving tank 6 provided in parallel for temporarily storing the culture solution 20 containing the bacterial cells in the culture tank 17, and the respective tanks. Liquid level sensors 5 and 10 for detecting the culture liquid level inside, a transfer pipe 11 for transferring the culture liquid from the culture tank 17 to the tanks 1 and 6, and a discharge pipe 13 for discharging the culture liquid in each tank. A compressed gas introduction pipe 12 for introducing compressed gas into each tank, a gas discharge pipe 24 for discharging gas in each tank, a pressure sensor 16 for detecting the pressure of the compressed gas, and the transfer pipe 11
The transfer control valve 2 for the first transfer receiving tank and the transfer control valve 7 for the second transfer receiving tank, and the discharge adjusting valves 4 and 2 for the first transfer receiving tank provided in the discharge pipe 13.
Discharge control valve 9 of the transfer receiving tank and pressure-feeding gas introduction pipe 12
Of the first transfer receiving tank and the pressure transfer gas adjusting valve 8 of the second transfer receiving tank, and the gas discharge adjusting valve 22 of the first transfer receiving tank provided in the gas discharge pipe 24 and The gas discharge control valve 23 of the second transfer tank and the control valves 2, 7, 4, 9 of the first transfer receiving tank and the second transfer receiving tank based on the signals of the liquid level sensors 5, 10 and the pressure sensor 16 described above. 3, 8, 22, 23, and a control device 15 for adjusting the pressure of the pressure-fed gas.
【0008】このような構成において、まず培養槽17
内の培養液20は、第1移送受タンク1に移送され、一
時的に貯溜される。このときの各調節弁の開閉は制御装
置15により、第1移送受タンク1の移送調節弁2とガ
ス排出調節弁22は開、排出調節弁3と圧送ガス調節弁
4は閉、第2移送受タンク6の移送調節弁7、排出調節
弁8、圧送ガス調節弁9およびガス排出調節弁23は閉
に制御される。In such a structure, first, the culture tank 17
The culture solution 20 therein is transferred to the first transfer receiving tank 1 and temporarily stored therein. The opening and closing of each control valve at this time is controlled by the controller 15 so that the transfer control valve 2 and the gas discharge control valve 22 of the first transfer receiving tank 1 are opened, the discharge control valve 3 and the pressurized gas control valve 4 are closed, and the second transfer is performed. The transfer control valve 7, the discharge control valve 8, the pressure-feed gas control valve 9 and the gas discharge control valve 23 of the receiving tank 6 are controlled to be closed.
【0009】次に第1移送受タンク1内の培養液面が一
定の高レベルに達すると、液面センサー5の信号が制御
装置15に送られ、該制御装置15の信号により、第1
移送受タンク1の移送調節弁2とガス排出調節弁22が
閉、排出調節弁3と圧送ガス調節弁4が開に変更され、
第1移送受タンク1への培養液の移送が停止され、圧送
ガスが導入されて該タンク1から培養液が排出される。
同時に第2移送受タンク6の移送調節弁7とガス排出調
節弁23が開、排出調節弁8と圧送ガス調節弁9が閉に
変更され、第2移送受タンク6への培養槽17から培養
液の移送が開始される。このときの各調節弁の開閉状態
を図1に示した。Next, when the culture liquid level in the first transfer receiving tank 1 reaches a certain high level, the signal of the liquid level sensor 5 is sent to the control device 15, and the signal of the control device 15 causes the first
The transfer control valve 2 and the gas discharge control valve 22 of the transfer receiving tank 1 are closed, and the discharge control valve 3 and the pressure-feed gas control valve 4 are changed to open,
The transfer of the culture solution to the first transfer receiving tank 1 is stopped, the pressure-fed gas is introduced, and the culture solution is discharged from the tank 1.
At the same time, the transfer control valve 7 and the gas discharge control valve 23 of the second transfer receiving tank 6 are changed to open, and the discharge control valve 8 and the pressure-feeding gas control valve 9 are changed to closed, so that the culture from the culture tank 17 to the second transfer receiving tank 6 is started. The liquid transfer is started. The open / closed state of each control valve at this time is shown in FIG.
【0010】さらに第1移送受タンク1の培養液面が一
定の低レベルに達すると、液面センサー5の信号が制御
装置15に送られ、該制御装置15の信号により、上記
開閉状態とは逆の状態に変更される。すなわち、第1移
送受タンク1の移送調節弁2とガス排出調節弁22が
開、排出調節弁3と圧送ガス調節弁4が閉、および第2
移送受タンク6の移送調節弁7とガス排出調節弁23が
閉、排出調節弁8と圧送ガス9が開に変更され、第2移
送受タンク6への培養液の移送が停止され、圧送ガスが
導入されて該タンクから培養液が排出され、同時に第1
移送受タンク1には培養槽17から培養液が移送されて
貯溜される。以下同様の操作を順に繰り返すことによ
り、培養液20は、培養槽17から移送先へ連続的に移
送される。Further, when the culture liquid level of the first transfer receiving tank 1 reaches a certain low level, a signal from the liquid level sensor 5 is sent to the control device 15, and the signal from the control device 15 causes the open / closed state. It is changed to the opposite state. That is, the transfer control valve 2 and the gas discharge control valve 22 of the first transfer receiving tank 1 are opened, the discharge control valve 3 and the pressure-feed gas control valve 4 are closed, and the second
The transfer control valve 7 and the gas discharge control valve 23 of the transfer receiving tank 6 are closed, the discharge control valve 8 and the pressure-feeding gas 9 are changed to open, the transfer of the culture solution to the second transfer receiving tank 6 is stopped, and the pressure-feeding gas is transferred. Is introduced and the culture solution is discharged from the tank.
The culture solution is transferred from the culture tank 17 and stored in the transfer receiving tank 1. The culture solution 20 is continuously transferred from the culture tank 17 to the transfer destination by sequentially repeating the same operation.
【0011】このような培養液移送装置では、並列に設
けられた2以上の移送タンクの培養液の貯溜および排出
を各調節弁の開閉および圧送ガスの圧力を調節して順に
繰り返して行うことにより、機械的な駆動駆動を用いる
ことなく加圧ガスによる静圧下で培養液を連続的に移送
できるため、培養液中の菌体の形態維持が容易となり、
従来のように移送中に菌体が切断され、増殖が阻害され
ることがなくなる。またこのような移送装置は、培養液
の移送だけでなく、強度の弱い樹脂粒子を含む固液スラ
リの搬送、例えば液体クロマトグラフィー用充填剤のカ
ラムへの充填操作等に適用することができる。In such a culture medium transfer device, the storage and discharge of the culture liquid in two or more transfer tanks provided in parallel are repeated in order by opening / closing each control valve and adjusting the pressure of the pressure-fed gas. Since the culture solution can be continuously transferred under the static pressure of the pressurized gas without using mechanical drive, it becomes easy to maintain the morphology of the bacterial cells in the culture solution,
Unlike the conventional method, the bacterial cells are not cut during the transfer and the growth is not inhibited. Further, such a transfer device can be applied not only to transfer of a culture solution, but also to transfer of a solid-liquid slurry containing resin particles having low strength, for example, a packing operation of a packing material for liquid chromatography into a column.
【0012】[0012]
【実施例】以下、本発明を実施例により説明するが、本
発明はこれらに限定されるものではない。 実施例1 供試菌体Anabaena sp.(ラン藻)を25℃
の改変デトマー培地中で培養し、得られた培養液(菌体
濃度1.0g/l)3リットルを、図1に示す2連式の
培養液移送装置を用いて24時間連続してリサイクル移
送を行った。リサイクル移送は図1の排出配管13を培
養槽17に連結した循環ラインを設けることにより行っ
た。移送受タンクの容量は5リットルで、移送容量は1
0リットル/min (5リットル/30sec /Batc
h)であった。また圧送ガスとしては空気を用い、圧力
2kg/cm2 Gで導入した。リサイクル移送における
培養液中の蛋白量の変化を調べ、その結果を図2に示し
たが、移送中にこれらの量の変化はみられず、培養液中
の菌体が破損していないことがわかった。また24時間
後の培養液中の菌体の形態を顕微鏡で観察したが、菌体
の切断は見られなかった。EXAMPLES The present invention will be described below with reference to examples, but the present invention is not limited thereto. Example 1 Test bacterial cells Anabaena sp. (Cyanobacteria) at 25 ℃
3 liters of the resulting culture solution (cell concentration: 1.0 g / l) was cultivated in the modified detomer medium described in Example 1 and continuously recycled for 24 hours using the double-type culture solution transfer device shown in FIG. I went. The recycling transfer was performed by providing a circulation line connecting the discharge pipe 13 of FIG. 1 to the culture tank 17. The transfer tank has a capacity of 5 liters and a transfer capacity of 1
0 liter / min (5 liter / 30 sec / Batc
h). Air was used as the pressure-feeding gas, and the gas was introduced at a pressure of 2 kg / cm 2 G. The changes in the amount of protein in the culture solution during the recycle transfer were examined, and the results are shown in Fig. 2. These changes were not observed during the transfer, indicating that the bacterial cells in the culture solution were not damaged. all right. Further, the morphology of the bacterial cells in the culture medium after 24 hours was observed with a microscope, but no cutting of the bacterial cells was observed.
【0013】比較例1 実施例1と同様の培養液3リットルを、図3に示すよう
に、遠心ポンプ(イワキマグネットポンプ社製、10リ
ットル/min 、100V、ケーシングおよびインペラ
ー:カーボン繊維強化ポリプロピレン)21を用いて連
続リサイクル移送を24時間行った。実施例1と同様に
培養液中の蛋白量の変化を調べ、その結果を図2に示し
たが、蛋白量が時間の経過に伴って増大し、培養液中の
菌体が破損していることがわかった。また24時間後の
培養液中の菌体の形態を顕微鏡で観察したが、菌体は切
断されており、実施例1で得られた菌体より1/2〜1
/4程度短いものであった。Comparative Example 1 As shown in FIG. 3, a centrifugal pump (Iwaki Magnet Pump Co., Ltd., 10 l / min, 100 V, casing and impeller: carbon fiber reinforced polypropylene) was added to 3 l of the same culture solution as in Example 1. 21 was used for continuous recycle transfer for 24 hours. The change in the amount of protein in the culture solution was examined in the same manner as in Example 1, and the results are shown in FIG. 2. The amount of protein increased with the passage of time, and the bacterial cells in the culture solution were damaged. I understand. In addition, the morphology of the bacterial cells in the culture solution after 24 hours was observed with a microscope. The bacterial cells were cut, and the bacterial cells obtained in Example 1 were 1/2 to 1 times.
It was about / 4 short.
【0014】[0014]
【発明の効果】本発明によれば、機械的な駆動手段を用
いることなく静圧下で培養液を連続的に移送できるた
め、培養液中の菌体の形態維持が容易であり、従来のよ
うに移送中に菌体が切断され、増殖が阻害されることが
ない。According to the present invention, since the culture solution can be continuously transferred under static pressure without using a mechanical driving means, it is easy to maintain the morphology of the bacterial cells in the culture solution. The cells are not cut during the transfer to the cell and the growth is not inhibited.
【図1】本発明の一実施例を示す培養液移送装置の説明
図。FIG. 1 is an explanatory view of a culture medium transfer device showing an embodiment of the present invention.
【図2】実施例1または比較例1における移送時の培養
液中の蛋白量の変化を示す図。FIG. 2 is a graph showing changes in the amount of protein in the culture medium during transfer in Example 1 or Comparative Example 1.
【図3】比較例1で用いた培養液移送装置の説明図。FIG. 3 is an explanatory diagram of a culture medium transfer device used in Comparative Example 1.
1…第1移送受タンク、2、7…移送調節弁、3、8…
圧送ガス調節弁、4、9…排出調節弁、5、10…液面
センサー、6…第2移送受タンク、11…移送配管、1
2…圧送ガス導入管、13…排出配管、15…制御装
置、16…圧力センサー、17…培養槽、20…培養
液、21…遠心ポンプ、22、23…ガス排出調節弁、
24…ガス排出管。1 ... 1st transfer receiving tank, 2, 7 ... Transfer control valve, 3, 8 ...
Pressure feeding gas control valve, 4, 9 ... Discharge control valve, 5, 10 ... Liquid level sensor, 6 ... Second transfer receiving tank, 11 ... Transfer pipe, 1
2 ... Pressure-feeding gas introduction pipe, 13 ... Exhaust pipe, 15 ... Control device, 16 ... Pressure sensor, 17 ... Culture tank, 20 ... Culture liquid, 21 ... Centrifugal pump, 22, 23 ... Gas discharge control valve,
24 ... Gas exhaust pipe.
Claims (1)
貯溜する、並列に設けられた二以上の移送受タンクと、
該各移送受タンク内の培養液面を検出する液面センサー
と、上記培養槽から各移送受タンクに培養液を移送する
移送配管と、各移送受タンク内の培養液を排出する排出
配管と、各移送受タンク内に圧送ガスを導入する圧送ガ
ス導入配管、各移送受タンク内ガスを排出するガス排出
配管および圧送ガスの圧力を検出する圧力センサーと、
上記各移送受タンクの移送配管、排出配管、圧送ガス導
入配管およびガス排出配管にそれぞれ設けられた調節弁
と、上記各液面センサーおよび圧力センサーの信号に基
づき、各移送受タンクへの培養液の貯溜と各移送受タン
クからの培養液の排出を順次繰り返し行って培養液を連
続的に排出するように各調節弁の開閉および圧送ガスの
圧力を調節する制御装置とを備えたことを特徴とする培
養液移送装置。1. Two or more transfer receiving tanks arranged in parallel for temporarily storing a culture solution containing bacterial cells in a culture tank,
A liquid level sensor for detecting the surface of the culture solution in each transfer receiving tank, a transfer pipe for transferring the culture solution from the culture tank to each transfer receiving tank, and a discharge pipe for discharging the culture solution in each transfer receiving tank. A pressure-feeding gas introducing pipe for introducing the pressure-feeding gas into each transfer-receiving tank, a gas discharge pipe for discharging the gas in each transfer-receiving tank, and a pressure sensor for detecting the pressure of the pressure-feeding gas,
Based on the signals of the transfer pipes, discharge pipes, pressure-feeding gas introduction pipes and gas discharge pipes of the transfer receiving tanks, and the signals of the liquid level sensors and pressure sensors, the culture solution to the transfer receiving tanks. And a control device that controls the opening and closing of each control valve and the pressure of the pressure-fed gas so that the culture solution is continuously discharged by sequentially and repeatedly storing the culture solution and discharging the culture solution from each transfer receiving tank. And a culture medium transfer device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18220694A JPH0838157A (en) | 1994-08-03 | 1994-08-03 | Culture solution conveyer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18220694A JPH0838157A (en) | 1994-08-03 | 1994-08-03 | Culture solution conveyer |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0838157A true JPH0838157A (en) | 1996-02-13 |
Family
ID=16114215
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18220694A Pending JPH0838157A (en) | 1994-08-03 | 1994-08-03 | Culture solution conveyer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0838157A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002531114A (en) * | 1998-12-04 | 2002-09-24 | インスティチュート・パスツール | Method and apparatus for selecting accelerated growth of living cells in suspension |
JP2006109707A (en) * | 2004-10-12 | 2006-04-27 | Hiroshima Univ | Apparatus for cell culture |
JP2007247175A (en) * | 2006-03-14 | 2007-09-27 | Shinwa Techno:Kk | Grouting method |
JP2017000003A (en) * | 2015-06-04 | 2017-01-05 | 澁谷工業株式会社 | Apparatus for supplying cell suspension |
-
1994
- 1994-08-03 JP JP18220694A patent/JPH0838157A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002531114A (en) * | 1998-12-04 | 2002-09-24 | インスティチュート・パスツール | Method and apparatus for selecting accelerated growth of living cells in suspension |
JP2006109707A (en) * | 2004-10-12 | 2006-04-27 | Hiroshima Univ | Apparatus for cell culture |
JP2007247175A (en) * | 2006-03-14 | 2007-09-27 | Shinwa Techno:Kk | Grouting method |
JP2017000003A (en) * | 2015-06-04 | 2017-01-05 | 澁谷工業株式会社 | Apparatus for supplying cell suspension |
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