JPH01206988A - Culture apparatus - Google Patents

Culture apparatus

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Publication number
JPH01206988A
JPH01206988A JP3164688A JP3164688A JPH01206988A JP H01206988 A JPH01206988 A JP H01206988A JP 3164688 A JP3164688 A JP 3164688A JP 3164688 A JP3164688 A JP 3164688A JP H01206988 A JPH01206988 A JP H01206988A
Authority
JP
Japan
Prior art keywords
culture
filter
tank
liquid
solution
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
JP3164688A
Other languages
Japanese (ja)
Other versions
JPH0734736B2 (en
Inventor
Koichi Yamagata
浩一 山形
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.)
Shimadzu Corp
Original Assignee
Shimadzu Corp
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 Shimadzu Corp filed Critical Shimadzu Corp
Priority to JP3164688A priority Critical patent/JPH0734736B2/en
Publication of JPH01206988A publication Critical patent/JPH01206988A/en
Publication of JPH0734736B2 publication Critical patent/JPH0734736B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To provide the title apparatus so designed that a bypass channel for temporarily bypassing a culture solution externally is provided and fitted with a cylinder with a special filter included, thereby efficiently taking out cell aggregates consisting mainly of dead cells from said solution. CONSTITUTION:In a culture apparatus designed to perform culture by making cells float on a liquid culture medium, a culture tank 2 is connected to a fresh culture medium feed means 4 and provided with a circulation system comprising a drawing pipe b1 for culture solution, a specific pump 51, a valve 52, a filter 53 and a feedback pipe b2. The filter 53 is fitted with a filter impermeable for cells to return them to the tank 2, and the dissolved components in the culture solution are put into a withdrawal vessel 55 either singly or together with said solution. Said circulation system is provided with a bypass channel C having such a structure that a valve 61, a filter 63 and another valve 62 are connected in this order from either side of the valve 52 through a pipe channel. The filter 63 is fitted with a filter impermeable for cell aggregates, and when cell aggregates are accumulated to some extent in its upstream side, the valves 61, 62 are closed to subject a washing liquid to back-flow fro a vessel 64 to the filter 63, thus collecting said aggregates together with the washing liquid into a vessel 67.

Description

【発明の詳細な説明】 (イ)産業上の利用分野 この発明は培養装置に関する。さらに詳しくは高密度お
よび連続培養に好適な培養装置に関する。
DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application This invention relates to a culture device. More specifically, the present invention relates to a culture device suitable for high-density and continuous culture.

(ロ)従来の技術 従来動物細胞等を大量培養しようとする場合に、小さな
装置で効率良く培養するためには培養液中から老廃物を
多く含んだ培地を連続かつ高速でかつ確実に回収するこ
とが必要であり、このため培養液交換手段を備えた培養
装置か用いられている。
(B) Conventional technology Conventionally, when attempting to culture animal cells in large quantities, in order to efficiently culture them in a small device, it is necessary to continuously, rapidly, and reliably collect the medium containing many waste products from the culture solution. Therefore, a culture device equipped with a means for exchanging the culture medium is used.

とくに浮遊性の動物細胞の場合には、撹拌型の培!!槽
に培養液交換手段を取り付けた培養装置が用いられるこ
とが多い(杉野幸夫編、rm抱培養技術」 講談社、 
1985年、 p146〜150)。上記培養液交換手
段とは、培養槽内に設けた細胞沈殿管、培養槽内もしく
は培養槽に付設されろ培養液循環路に設けられた口過手
段等のごと<=m胞と培地とを分離しかっこの分離され
た培地を培養槽外に排出ずろ手段と、新鮮培地を培養槽
に供給する手段とを合わせたものをいう。
Especially in the case of planktonic animal cells, use a stirred culture medium! ! A culture device with a culture medium exchange means attached to the tank is often used (Yukio Sugino, ed., RM culture technology, Kodansha,
1985, p146-150). The above-mentioned culture solution exchange means include a cell sedimentation tube provided in the culture tank, a port passage means provided in the culture tank or a culture solution circulation path attached to the culture tank, etc. This refers to a combination of means for discharging the separated culture medium out of the culture tank and means for supplying fresh culture medium to the culture tank.

(ハ)発明が解決しようとする課題 連続的に培養を行うとやがて死んだ@抱が固まって細胞
塊をつくるが、この細胞塊は生さている細胞に比べて沈
降しやすい。従って細胞沈殿管を有する培養装置で培養
を行う場合、上記細胞塊は生きている細胞よりも培!I
漕外に排出されにくいため、培lll槽内には細胞塊が
どんどん溜まってきて細胞にとって好ましくない環境と
なる。また、培養槽内にもしくは培養槽に付設される培
養液循環路に口過手段とを有する培養装置で連続的に培
養を行うと、上記細胞塊によって口過手段の目詰まりが
はやくなり、培地の交換が十分に行えなくなる。
(c) Problems to be Solved by the Invention When cells are cultured continuously, dead cells eventually solidify and form cell clusters, but these cell clusters tend to settle more easily than living cells. Therefore, when culturing is carried out in a culture device with a cell sedimentation tube, the above-mentioned cell clusters are more likely to be cultured than living cells. I
Since it is difficult to discharge the cells to the outside of the tank, cell clumps gradually accumulate in the culture tank, creating an unfavorable environment for the cells. Furthermore, when culturing is carried out continuously in a culture device having a passage means in a culture tank or a culture solution circulation path attached to a culture tank, the passage means is quickly clogged by the cell mass, and the culture medium is replacement cannot be carried out adequately.

この発明はかかる状況に鑑みなされたものであり、培養
液中から細胞塊を除去しうろ手段を有して安定した連続
培養が行えるよう構成された培養装置を提供しようとす
るものである。
The present invention has been made in view of the above situation, and it is an object of the present invention to provide a culture device that is configured to have a means for removing cell clusters from the culture solution and to perform stable continuous culture.

(ニ)課題を解決するための手段 かくしてこの発明によれば、細胞等を含んだ培養液を循
環または貯留して細胞等の増殖を行う培養系と、該培養
系中の液状培地を連続的に新鮮培地と交換しうる液−補
給・分離手段を備え、上記培養系に、培養液を一時この
系外に迂回できろ迂回流路を設けると共に、該迂回流路
に、培養液中の細胞等を透過するが細胞塊等を透過しえ
ないフィルタを内蔵した筒状体からなり、このフィルタ
により分割される筒状体内下流側に洗浄液供給手段を管
路接続し、かつ上記筒状体内上流側にドレインへの排出
管路を接続して構成される細胞塊除去部を挿設してなる
培養装置が提供されろ。
(d) Means for Solving the Problems Thus, according to the present invention, there is provided a culture system in which a culture solution containing cells, etc. is circulated or stored to grow cells, etc., and a liquid medium in the culture system is continuously maintained. The culture system is equipped with a liquid replenishment/separation means that can be exchanged with a fresh medium, and the culture system is provided with a detour flow path through which the culture medium can be temporarily bypassed outside the system, and the detour flow path is provided with a means for replenishing and separating the culture medium. A cleaning liquid supply means is connected to the downstream side of the cylindrical body divided by the filter, and a cleaning liquid supply means is connected to the upstream side of the cylindrical body. There should be provided a culture device in which a cell mass removal section is inserted on the side of the cell clump, which is configured by connecting a discharge pipe to a drain.

この発明は、培養操作を停止することなく必要に応じて
培養液中に生じた細胞塊を効率良く除去できうるよう構
成された培養装置であることを特徴とする。
The present invention is characterized in that it is a culture apparatus configured to be able to efficiently remove cell clusters generated in a culture solution as needed without stopping the culture operation.

この発明の培養装置は、連続的かつ高密度培養に好適な
装置であり、さらにバイオリアクタにも適用できる乙の
である。
The culture device of the present invention is suitable for continuous and high-density culture, and can also be applied to bioreactors.

この発明の培養装置において、細胞等を含んだ培養液を
循環または貯留して細胞等の増殖を行う培養系とは、上
記培養液を循環または貯留でき、かつ撹拌手段、液面セ
ンサ、p t−iメータ等培養に必要な部材が必要に応
じて具備された当該分野で公知の培flF!またはこれ
と均等な機能を備えた培養槽を意味する。また、この発
明の培養装置に具備される液−補給・分離手段としては
、公知のもの例えば、培養槽内に設けた細胞沈殿管、培
養槽内らしくは培illに付設される培養液循環路に設
けられた口過部等のごとく細胞と液状培地とを分離しか
つこの分離された培地を培!!漕外に排出する手段と、
新鮮培地供給手段とからなるもの等をそのまま用いるこ
とができる。
In the culture apparatus of the present invention, a culture system that circulates or stores a culture solution containing cells, etc. to grow cells, etc. is a culture system that can circulate or store the culture solution, and includes a stirring means, a liquid level sensor, and a pt. - A culture flF known in the field that is equipped with necessary parts for culture such as an i-meter! Or means a culture tank with equivalent functions. In addition, as the liquid replenishment/separation means included in the culture apparatus of the present invention, known ones may be used, such as a cell sedimentation tube provided in the culture tank, and a culture liquid circulation path attached to the culture tank or culture tank. Separate the cells from the liquid medium using a mouth opening, etc., and culture this separated medium! ! means for discharging outside the tank;
A means for supplying a fresh culture medium can be used as is.

この発明の培養装置において培養系に設けられる培養液
迂回流路は、培養系外に一時培養液を迂回できるように
構成されたものであり、送液手段を介して培養系内と該
系外との間を培養液を循環できるように構成される。こ
の迂回流路は培養槽に直接設けられてもよく、また上記
液−補給・分離手段の分離手段に設けられてもよい。後
者の場合において分離手段側か口過部を有して培養槽に
付設された培養液循環路で構成されているとき、上記迂
回流路は、培養液循環路の口過部の前段に設けられ、か
つ迂回流路と培養液循環路との流路切換手段が設定され
る。なおこのとき迂回流路に設定される送液手段は培養
液循環路に設定されている送液手段と共通であってもよ
い。この構成の一例については後述する実施例の記載が
参照される。
In the culture device of the present invention, the culture solution bypass flow path provided in the culture system is configured to temporarily bypass the culture solution to outside the culture system, and is configured to temporarily bypass the culture solution to the inside and outside of the culture system through the liquid feeding means. The structure is such that the culture solution can be circulated between the This detour channel may be provided directly in the culture tank, or may be provided in the separation means of the liquid replenishment/separation means. In the latter case, when the separation means side is configured with a culture solution circulation path attached to the culture tank with an opening section, the detour channel is provided before the opening section of the culture solution circulation path. and a flow path switching means between the detour flow path and the culture solution circulation path is set. Note that at this time, the liquid feeding means set in the detour channel may be the same as the liquid feeding means set in the culture solution circulation path. For an example of this configuration, refer to the description of the embodiment described later.

上記培養液迂回流路には細胞塊除去手段が設けられる。A cell mass removing means is provided in the culture solution detour channel.

この細胞塊除去手段は上記迂回流路への流路接続が可能
な液導入口および液排出口を対向する端面に宵する筒状
体と、該筒状体内部の断面にわたって設けられるフィル
タと、このフィルタにより分割される筒状体内下流側に
管路接続される洗浄液供給手段と、上記筒状体内下流側
に接続されるドレインへの排出管路とから主として構成
される。上記フィルタは培養液中の細胞等を透過するが
細胞塊等を透過しえない程度の網目状のものが選択され
る。この網目の孔径としては約0.5〜2mI+1が適
している。上記筒状体の材質としては該筒状体外部から
その内部を透視できうるらのが好ましく、これにはガラ
スまたは透明樹脂が適し、一方フィルタの材質としては
ステンレス、合成樹脂が選択され、合成樹脂としてはナ
イロンが好ましい。上記筒状体内下流側に管路接続され
る洗浄液供給手段は、送液ポンプを介して洗浄液貯留槽
に接続される管路から構成されるものが好ましい。
This cell mass removal means includes a cylindrical body having a liquid inlet port and a liquid discharge port on opposite end faces, which can be connected to the bypass flow path, and a filter provided over a cross section inside the cylindrical body. It mainly consists of a cleaning liquid supply means connected to the downstream side of the cylindrical body divided by the filter, and a discharge conduit to a drain connected to the downstream side of the cylindrical body. The filter is selected to have a mesh shape that allows it to pass through cells and the like in the culture medium but not through cell clusters and the like. A suitable pore size for this mesh is approximately 0.5 to 2 mI+1. The material of the cylindrical body is preferably one that allows the inside to be seen through from the outside of the cylindrical body, and glass or transparent resin is suitable for this, while the material of the filter is selected from stainless steel, synthetic resin, and synthetic resin. Nylon is preferred as the resin. It is preferable that the cleaning liquid supply means connected to the downstream side of the cylindrical body by a pipeline is constituted by a pipeline connected to the cleaning liquid storage tank via a liquid feeding pump.

一方上記筒状体内上流側に接続される排出管路には流路
開閉弁が設けられる。
On the other hand, a flow path opening/closing valve is provided in the discharge pipe connected to the upstream side of the cylindrical body.

この発明の装置において、迂回流路への培養液の移送の
タイミングは、目視に基づく培養槽内で′の細胞塊の生
成状態に基づいて手動で行うものであってもよく、また
所定時間毎に機械的に作動しうるよう予め設定されたプ
ログラムにより切換操作が制御されていてらよい。また
、迂回流路に挿設される細胞塊除去手段への洗浄液供給
のタイミングは、目視に基づく筒状体内の細胞塊の蓄積
状態に応じて手動で行うものであってもよく、所定時間
毎に機械的に作動しうるよう予め設定されたプログラム
により切換操作が制御されていてもよい。またさらにこ
のタイミングに関する別の構成としては、上記除去部に
内蔵されるフィルタの上流側流路および下流側流路にそ
れぞれ圧力計を取り付け、該フィルタの目詰まり状態を
両者の圧力変動により自動的に感知して行う構成であっ
てもよい。
In the apparatus of the present invention, the timing of transferring the culture medium to the detour channel may be manually based on the state of cell mass formation in the culture tank based on visual observation, or may be carried out at predetermined intervals. The switching operation may be controlled by a preset program that can be mechanically operated. Furthermore, the timing of supplying the cleaning liquid to the cell mass removal means inserted in the detour channel may be performed manually depending on the state of accumulation of cell mass inside the cylindrical body based on visual observation, and the cleaning solution may be supplied at predetermined intervals. The switching operation may be controlled by a preset program that can be mechanically operated. Furthermore, as another configuration regarding this timing, a pressure gauge is attached to each of the upstream flow path and the downstream flow path of the filter built in the removal section, and the clogging state of the filter is automatically detected by pressure fluctuations in both. It may also be configured to perform this by sensing.

(ホ)作用 この発明によれば、培養系から増殖細胞、細胞塊、液状
培地等を含有してこの培養系外に迂回される培養液は、
迂回流路の途中に設けられた細胞塊除去部のフィルタに
おいて細胞塊のみが口5ji+された後、上記培養系内
に戻される。上記フィルタにおいて口利された細胞腕が
ある程度蓄積すると培養系からの培養液の迂回流路への
移送は停止されると共に、この除去部内の下流側に洗浄
液が供給されさらにこの洗浄液がフィルタを介して上流
側に逆流され、この上流部に蓄積されている細胞塊と共
に排出管路を通じてドレインへ排出される。
(E) Effect According to the present invention, the culture solution containing proliferating cells, cell masses, liquid medium, etc. and bypassed from the culture system to the outside of the culture system is
After only the cell aggregates are filtered through the filter of the cell aggregate removal section provided in the middle of the detour channel, they are returned to the culture system. When the cell arms harvested in the filter accumulate to a certain extent, the transfer of the culture solution from the culture system to the detour channel is stopped, and a washing solution is supplied to the downstream side of this removal section, and this washing solution is further passed through the filter. The cell mass is then flowed back upstream, and is discharged to the drain through the discharge pipe along with the cell mass accumulated in this upstream section.

以下実施例によりこの発明の詳細な説明するが、これに
よりこの発明は限定される乙のではない。
The present invention will be described in detail below with reference to Examples, but the present invention is not limited thereby.

(へ)実施例 第1図はこの発明の培養装置の一実施例の構成説明図で
ある。図において培養装置(1)は、培養槽(2)、撹
拌手段(3)、新鮮培地供給手段(4)、培養液口過手
段(5)、細胞塊除去手段(6)、制御部(7)から主
として構成されている。
(F) Embodiment FIG. 1 is an explanatory diagram of the configuration of an embodiment of the culture apparatus of the present invention. In the figure, the culture device (1) includes a culture tank (2), stirring means (3), fresh medium supply means (4), culture liquid filtration means (5), cell mass removal means (6), and control section (7). ).

培養槽(2)は、培養液貯留槽とこれを着脱可能に密閉
しうる蓋体とから構成されている。該蓋体には液面セン
サ(21)、撹拌羽根(31)、図示しないpH1を極
、図示しないDoセンサおよび後述する各管路がそれぞ
れ所定の位置に設定されて″いる。
The culture tank (2) is composed of a culture solution storage tank and a lid that can removably seal the tank. A liquid level sensor (21), a stirring blade (31), a pH1 pole (not shown), a Do sensor (not shown), and each pipe line described later are set at predetermined positions on the lid.

またこの培!l漕には図示しない温度コントローラが付
設されており培養液の温度が所定の温度で一定に保持で
きるように構成されている。
This cultivation again! A temperature controller (not shown) is attached to the tank so that the temperature of the culture solution can be kept constant at a predetermined temperature.

撹拌手段(3)は、上記撹拌羽根(31)とこれを回転
する図示しない回転駆動部とから構成されている。
The stirring means (3) is composed of the stirring blade (31) and a rotation drive unit (not shown) that rotates the stirring blade (31).

新鮮培地供給手段(4)は、新鮮培地を貯留する培地タ
ンク(41)と該タンク内の底部近傍に開口し、ペリス
タポンプ(42)を介して培養111(2)の蓋体に接
続され、培養槽内の上部空間に開口する培地供給管路(
a)とから構成されている。
The fresh medium supply means (4) opens near the bottom of a medium tank (41) that stores fresh medium, and is connected to the lid of the culture 111 (2) via a peristaltic pump (42), and Culture medium supply pipe opening into the upper space in the tank (
It consists of a).

培養液口過手段(5)は、培養槽内の底部近傍に開口し
て蓋体に取り付けられ、ペリスタポンプ(51)および
電磁弁(52)をこの順に介して口過部(53)上端に
管路接続される汲み出し管路(b、)と、該口過部(5
3)下端から再び上記蓋体に接続されて培養槽内の上部
空間に開口して設定される戻し管路(b、)と、上記口
過部(53)側面下部からペリスタポンプ(54)を介
して回収タンク(55)に管路接続される回収管路(b
3)とから構成されて(Yろ。上記汲み出し管路(bυ
と戻し管路(b、)とで培養液循環路(b)が構成され
ている。上記口過部(53)には、筒状にフィルタ面を
有して流路と同軸に設定されるフィルタ管路と、このフ
ィルタ管路の外側にフィルタ管路内からの透過液を一時
貯留する外筒状容器とから構成されるクロスフロー型口
過装置が用いられている。上記フィルタ面のフィルタ孔
径は、細胞等を透過しないが培養液中の溶解成分を透過
しうる孔径のもの(例えば0.2〜10μm程度)が用
いられている。
The culture liquid passage means (5) opens near the bottom of the culture tank and is attached to the lid, and connects a pipe to the upper end of the mouth passage part (53) through a peristaltic pump (51) and a solenoid valve (52) in this order. The pumping pipe (b,) connected to the pipe and the mouth part (5)
3) A return pipe (b,) which is connected to the lid again from the lower end and opened to the upper space in the culture tank, and a peristaltic pump (54) from the lower side of the mouth part (53). A recovery pipe (b) is connected to the recovery tank (55).
3) and (Y). The above pumping pipe (bυ
The culture solution circulation path (b) is constituted by the return pipe (b,) and the return pipe (b,). The mouth passage part (53) includes a filter pipe having a cylindrical filter surface and set coaxially with the flow path, and a permeate from inside the filter pipe is temporarily stored on the outside of this filter pipe. A cross-flow type gating device is used, which consists of an outer cylindrical container. The filter pore size of the filter surface used is a pore size (for example, about 0.2 to 10 μm) that does not allow cells to pass through, but allows dissolved components in the culture solution to pass through.

細胞塊除去手段(6)は、上記培養液口過手段(5)の
汲み出し管路(bl)の電磁弁(52)の上流側に管路
接続され、II電磁弁61)およびII&!弁(62)
をこの順に介して再び汲み出し管路(b、)の電磁弁(
52)の下流側に管路接続される迂回管路(c)と、こ
の迂回管路(e)に挿設された細胞塊除去ユニット(6
3)と、洗浄液タンク(64)からペリスタポンプ(6
5)を介して上記細胞塊除去ユニッ) (63)の下流
側に接続される洗浄液供給管路(dl)および細胞塊除
去ユニッ) (63)の上流側から電磁弁(66)を介
して洗浄液回収タンク(67)に接続される回収管路(
d2)とからなる細胞塊除去部(68)とから構成され
ている。
The cell mass removing means (6) is connected to the upstream side of the solenoid valve (52) of the pumping conduit (bl) of the culture liquid filtration means (5), and includes II solenoid valve 61) and II&! Valve (62)
In this order, pump out again through the solenoid valve (b,) of the pipe (b,).
52), and a cell mass removal unit (6) inserted into this detour pipe (e).
3) and the peristaltic pump (6) from the cleaning liquid tank (64).
5) to the washing liquid supply pipe (DL) connected to the downstream side of the cell lump removal unit (63) and the washing liquid from the upstream side of the cell lump removal unit (63) via the solenoid valve (66). Recovery pipe (67) connected to recovery tank (67)
d2) and a cell mass removing section (68).

上記細胞塊除去ユニット(63)の構成の一例を第2図
に示す。この細胞塊除去ユニット(63)は図に示すご
とく、迂回管路(c)に接続可能な管路(e)を一端面
に有しかつ他端が外側に広げられた縁部を有して開口さ
れた円筒型容器体(8)の一対からなり、これらの開d
端面周縁を対向配置してこの間に所定のメツシュを有す
る網状フィルタ(9)をその両側から0リング(10)
(11)を介して密着挟持さ什ると共に、上記対向配置
された一対の開口周縁部の外周に沿って跨設された止め
バンド(12)により上記密着挟持状聾が保持されてい
る。上記のごとく構成される細胞塊除去ユニット(63
)において1、迂回管路(c)の上流側に接続される円
筒型容器体(以下液導入側部(イ))および迂回管路(
c)の下流側に接続される円筒型容器体(以下液排出側
部(ロ))それぞれには連通孔(81)(82)が設定
されている。このうち液排出側部(ロ)の連通孔(82
)に上記洗浄液逆流手段(68)の管路(dυが一接続
され、−方の液導入側部(イ)の連通孔(81)には洗
浄液逆流手段(68)の管路(d、)が接続されている
。上記網状フィルタ(9)はメツシュが2m+++のス
テンレス製のものであり、円筒型容器体(8)すなわち
液導入側部(イ)および液排出側部(ロ)はガラス製の
ものである。
An example of the configuration of the cell mass removal unit (63) is shown in FIG. 2. As shown in the figure, this cell mass removal unit (63) has a conduit (e) connectable to the detour conduit (c) on one end surface, and the other end has an outwardly expanded edge. Consisting of a pair of opened cylindrical container bodies (8), these openings d
A mesh filter (9) having a predetermined mesh between the edges of the end faces facing each other is inserted into an O-ring (10) from both sides.
(11), and is held by a retaining band (12) that extends along the outer periphery of the pair of opposing opening peripheries. Cell mass removal unit (63
), 1, a cylindrical container body (hereinafter referred to as liquid introduction side part (a)) connected to the upstream side of the detour pipe (c) and a detour pipe (
Communication holes (81) and (82) are set in each of the cylindrical container bodies (hereinafter referred to as liquid discharge side parts (b)) connected to the downstream side of c). Of these, the communication hole (82) on the liquid discharge side (b)
) is connected to the pipe line (dυ) of the cleaning liquid backflow means (68), and the communication hole (81) of the negative liquid introduction side (a) is connected to the pipe line (d,) of the cleaning liquid backflow means (68). The mesh filter (9) is made of stainless steel with a mesh of 2m+++, and the cylindrical container body (8), that is, the liquid introduction side (a) and the liquid discharge side (b) are made of glass. belongs to.

制御部(7)は、液面センサ(21)、撹拌手段(3)
、pH電極、DOセンサ、電磁弁(52)、(61)、
(62)。
The control section (7) includes a liquid level sensor (21) and a stirring means (3).
, pH electrode, DO sensor, solenoid valve (52), (61),
(62).

(66)、ペリスタポンプ(42)、(51)、(54
)、(65)にそれぞれ電気接続されており、これらを
予め設定された設定値に維持しまたは予め設定されたタ
イミングで駆動しうるプログラムを有し、このプログラ
ムに従って上記各部に作動を指令するよう構成されてい
る。
(66), peristaltic pump (42), (51), (54
) and (65), and has a program that can maintain these at preset values or drive them at preset timing, and instructs each of the above parts to operate according to this program. It is configured.

以上のごとく構成された培養装置(1)の作動を説明す
る。
The operation of the culture apparatus (1) configured as above will be explained.

まず通常の連続培養を行う場合、電磁弁(52)を開き
電磁弁(61)(62)および(66)を閉じておく。
First, when performing normal continuous culture, the solenoid valve (52) is opened and the solenoid valves (61), (62), and (66) are closed.

この状態でペリスタポンプ(51)および(54)をそ
れぞれ予め設定された速度で駆動すると、培II 漕(
2)内の培養液は所定量の送液量で、培養+! (2)
→管路(b、)−口過部(53)−管路(b、)−培養
槽(2)を循環される。この操作により該循環路上に設
定された口過部(53)において、培養液内の細胞等は
口過されず培養1(2)内に戻され、一方培養液中の溶
解成分は透過され回収管路(b、)を通じて回収タンク
(55)に回収される。この循環作動により培養液中で
細胞等が増殖されろと共にこの増殖に伴って生成され培
養液中に溶解した老廃物等は口過部(53)から除去さ
れ、培養槽内の液面が下降していくことになるが、この
液面が液面センナ(21)により検出されると制御部(
7)はこのセンサ(21)からの出力に基づいてペリス
タポンプ(42)を所定時間、所定の速度で駆動し、こ
れによって新鮮培地が所定量補給される。このようにし
て培養・増殖が連続して行われる。
In this state, when the peristaltic pumps (51) and (54) are driven at respective preset speeds, the culture medium II tank (
The culture solution in 2) is fed at a predetermined amount, and the culture +! (2)
→It is circulated through the pipe (b,) - the port (53) - the pipe (b,) - the culture tank (2). Through this operation, cells in the culture solution are returned to the culture 1 (2) without being passed through the mouth passage part (53) set on the circulation path, while dissolved components in the culture solution are permeated and collected. It is collected into the collection tank (55) through the pipe (b,). Due to this circulation operation, cells, etc. are multiplied in the culture medium, and waste products, etc., generated along with this multiplication and dissolved in the culture medium are removed from the mouth passage (53), and the liquid level in the culture tank is lowered. However, when this liquid level is detected by the liquid level sensor (21), the control unit (
7) drives the peristaltic pump (42) at a predetermined speed for a predetermined time based on the output from this sensor (21), thereby replenishing a predetermined amount of fresh culture medium. Cultivation and proliferation are performed continuously in this manner.

上記作動状態である程度進行すると培養液中に細胞塊が
生じ始めるが、これが目立ってくると目視に基づく切換
えか、または制御部内に設定したタイマ(培養開始から
所定時間経過後までの設定)の出力に基づく切換えによ
り、電磁弁(61)および(62)を開き一方電磁弁(
52)を閉じる。この状態においてペリスタポンプ(5
1)により汲み上げられる培養液は、管路(bl)の電
磁弁(52)の上流部から迂回管路(c)に流出されて
電磁弁(61)−細胞塊除去ユニット(63)−電磁弁
(62)の順に迂回して再び管路(bl)の電磁弁(5
2)の下流部に流入され、以下上記のごとく循環される
。この迂回循環により、培養液中の細胞塊は細胞塊除去
ユニット(63)内の液導入部側(イ)に口利され、一
方増殖対象の細胞等は該ユニット(63)内の網状フィ
ルタ(9)を通過して培1% 博(2)内に戻される。
When the above operating state progresses to a certain extent, cell clusters will begin to form in the culture solution, but when this becomes noticeable, the switch should be made based on visual inspection, or the output of a timer (set from the start of culture until after a predetermined time has elapsed) set in the control unit. By switching based on
52) Close. In this state, the peristaltic pump (5
The culture solution pumped up by 1) flows out from the upstream part of the solenoid valve (52) of the conduit (bl) to the detour conduit (c), and is passed through the solenoid valve (61) - cell mass removal unit (63) - solenoid valve. The solenoid valve (5) of the pipe (bl) is detoured again in the order of (62).
2) and then circulated as described above. Due to this detour circulation, cell aggregates in the culture solution are transferred to the liquid introduction part side (a) in the cell aggregate removal unit (63), while cells to be proliferated are transferred to the reticular filter (a) in the unit (63). 9) and returned to the 1% culture medium (2).

上記迂回循環の進行につれて細胞塊除去ユニッ) (6
3)の液導入部側(イ)に口利された細胞塊が蓄積しだ
すと、目視に基づいて、または液導入部側(イ)内およ
び液排出側(ロ)内の圧力を測定すべく設定された各圧
力センサの比較圧力値に基づいて、制御部からの指令に
より電磁弁(52)を開き電磁弁(61)および(63
)を閉じると同時に電磁弁(66)を開き、ペリスタポ
ンプ(65)を駆動する。この操作により培養液は再び
はじめのように培養液循環路を循環すると同時に、細胞
塊除去ユニット(63)に洗浄液タンク(64)から洗
浄液(この場合培地タンク(41)と同等の新鮮培地ま
たは等張の緩衝液)が、連通孔(82)−液排出側部(
ロ)−網状フィルタ(9)→液導入側部(イ)→連通孔
(81)の順に逆流され、電磁弁(66)を経て洗浄液
回収タンク(67)に回収される。この洗浄液逆流操作
により網状フィルタ(9)および液導入側部(イ)に蓄
積されていた細胞塊は、この洗浄液流によってこれらか
ら取り除かれて回収タンク(67)に排出され、細胞塊
は培養系外に除去されることとなる。その後目視による
判断または一定時間経過後の自動操作により、ペリスタ
ポンプ(65)を停止しかつ電磁弁(66)を閉じて洗
浄液逆流操作を終了して、再び通常の連続培養状態とす
る。
As the detour circulation progresses, the cell mass removal unit) (6
3) When the cell mass collected on the liquid inlet side (a) begins to accumulate, the pressure in the liquid inlet side (a) and the liquid outlet side (b) can be measured based on visual observation or the pressure inside the liquid inlet side (a) and the liquid outlet side (b). Based on the comparative pressure value of each pressure sensor that has been set, the solenoid valve (52) is opened by a command from the control unit and the solenoid valves (61) and (63) are opened.
) and at the same time open the solenoid valve (66) to drive the peristaltic pump (65). By this operation, the culture solution is circulated through the culture solution circulation path again as in the beginning, and at the same time, the cell mass removal unit (63) is transferred from the washing solution tank (64) to the washing solution (in this case, a fresh medium equivalent to the medium tank (41) or the like). (buffer solution) from the communication hole (82) to the liquid discharge side (
(b) - The liquid flows backward in the order of the mesh filter (9) -> the liquid introduction side part (a) -> the communication hole (81), and is collected in the cleaning liquid recovery tank (67) via the electromagnetic valve (66). Due to this washing liquid backflow operation, the cell clumps accumulated in the mesh filter (9) and the liquid introduction side part (a) are removed from them by this washing liquid flow and discharged into the recovery tank (67), and the cell clumps are removed from the culture system. It will be removed outside. Thereafter, by visual judgment or automatic operation after a certain period of time has elapsed, the peristaltic pump (65) is stopped and the solenoid valve (66) is closed to complete the washing liquid backflow operation and return to the normal continuous culture state.

従って上記操作が繰返されることにより、口過部(53
)での目詰まりが少なく長期間にわたって安定して連続
培養することができる。
Therefore, by repeating the above operation, the opening part (53
) with little clogging, allowing for stable and continuous culture over a long period of time.

(ト)発明の効果 この発明によればミ培養液に生ずる細胞塊を効率良く除
去でき、培養槽に付設される培養液循環路の口過部での
目詰まり等の不都合な状態か少なく培養液が培養に好ま
しい状態に保持できるので、安定した細胞培養を長時間
にわたって連続して行うことができる。
(G) Effects of the Invention According to the present invention, cell clusters generated in the culture solution can be efficiently removed, and inconvenient conditions such as clogging at the opening of the culture solution circulation path attached to the culture tank can be minimized. Since the liquid can be maintained in a state suitable for culture, stable cell culture can be carried out continuously over a long period of time.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はこの発明の培養装置の一実施例の構成説明図、
第2図は第1図の培養装置に用いられろ細胞塊除去ユニ
ットの一例の構成説明図である。 (2)・・・・・・培養槽、   (3)・・・・・・
撹拌手段、(4)・・・・・・新鮮培地供給手段、(5
)・・・・・・培養液口過手段、(6)・・・・・・細
胞塊除去手段、(7)・・・・・・制御部、    (
8)・・・・・・円筒型容器体、(9)・・・・・・網
状フィルタ、 (loXtt)・・・・・・0リング、
(12)・・・・・・止めバンド、 (21)・・・・・・液面センサ、 (3【)・・・・
・・撹拌羽根、(41)・・・・・・培地タンク、 (42X51X54)(65)・・・・・・ペリスタポ
ンプ、(52)(6106206B)・・・・・・電磁
弁、(53)・・・・・・口過部、”  (55)・・
・・・・回収タンク、(63)・・・・・・細胞塊除去
ユニット、(64)・・・・・・洗浄液タンク、 (67)・・・・・・洗浄液回収タンク、(68)・・
・・・・洗浄液逆流手段、(a)・・・・・・培地供給
管路、(b+)・・・・・・汲み出し管路、(b、)・
・・・・・戻し管路、  (c)・・・・・・迂回管路
。 第 1 図 第 2 図
FIG. 1 is an explanatory diagram of the configuration of an embodiment of the culture device of the present invention;
FIG. 2 is an explanatory diagram of the configuration of an example of a cell mass removal unit used in the culture apparatus of FIG. 1. (2)・・・・・・Culture tank, (3)・・・・・・
Stirring means, (4) Fresh medium supply means, (5
)・・・・・・Culture solution passing means, (6)・・・Cell mass removal means, (7)・・・Control unit, (
8)...Cylindrical container body, (9)...Mesh filter, (loXtt)...0 ring,
(12)...Stopping band, (21)...Liquid level sensor, (3[)...
... Stirring blade, (41) ... Culture medium tank, (42X51X54) (65) ... Peristaltic pump, (52) (6106206B) ... Solenoid valve, (53) ...・・・・・・Last part of the mouth," (55)...
...Recovery tank, (63) ...Cell mass removal unit, (64) ...Washing liquid tank, (67) ...Washing liquid recovery tank, (68)・
... Washing liquid backflow means, (a) ... Culture medium supply pipe line, (b+) ... Pumping pipe line, (b, ).
...Return pipe line, (c)...Detour pipe line. Figure 1 Figure 2

Claims (1)

【特許請求の範囲】 1、細胞等を含んだ培養液を循環または貯留して細胞等
の増殖を行う培養系と、該培養系中の液状培地を連続的
に新鮮培地と交換しうる液−補給・分離手段を備え、 上記培養系に、培養液を一時この系外に迂回できる迂回
流路を設けると共に、該迂回流路に、培養液中の細胞等
を透過するが細胞塊等を透過しえないフィルタを内蔵し
た筒状体からなり、このフィルタにより分割される筒状
体内下流側に洗浄液供給手段を管路接続し、かつ上記筒
状体内上流側にドレインへの排出管路を接続して構成さ
れる細胞塊除去部を挿設してなる培養装置。
[Scope of Claims] 1. A culture system in which cells, etc. are grown by circulating or storing a culture medium containing cells, etc., and a liquid medium in which the liquid medium in the culture system can be continuously replaced with fresh medium. The culture system is provided with a replenishment/separation means, and the culture system is provided with a bypass flow path that allows the culture solution to temporarily bypass the system, and the bypass flow path is provided with a bypass flow path that allows cells, etc. in the culture solution to pass through, but not cell clusters, etc. A cleaning liquid supply means is connected to the downstream side of the cylindrical body divided by the filter, and a discharge conduit to the drain is connected to the upstream side of the cylindrical body. A culture device in which a cell mass removal section is inserted.
JP3164688A 1988-02-12 1988-02-12 Incubator Expired - Fee Related JPH0734736B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3164688A JPH0734736B2 (en) 1988-02-12 1988-02-12 Incubator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3164688A JPH0734736B2 (en) 1988-02-12 1988-02-12 Incubator

Publications (2)

Publication Number Publication Date
JPH01206988A true JPH01206988A (en) 1989-08-21
JPH0734736B2 JPH0734736B2 (en) 1995-04-19

Family

ID=12336952

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3164688A Expired - Fee Related JPH0734736B2 (en) 1988-02-12 1988-02-12 Incubator

Country Status (1)

Country Link
JP (1) JPH0734736B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014528246A (en) * 2011-10-07 2014-10-27 ポール テクノロジー ユーケイ リミテッドPall Technology Uk Limited Fluid treatment control system and corresponding method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014528246A (en) * 2011-10-07 2014-10-27 ポール テクノロジー ユーケイ リミテッドPall Technology Uk Limited Fluid treatment control system and corresponding method
US10989362B2 (en) 2011-10-07 2021-04-27 Pall Technology Uk Limited Fluid processing control system and related methods

Also Published As

Publication number Publication date
JPH0734736B2 (en) 1995-04-19

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