JPH01273578A - Filtration method in continuous culture device and apparatus therefor - Google Patents
Filtration method in continuous culture device and apparatus thereforInfo
- Publication number
- JPH01273578A JPH01273578A JP63101926A JP10192688A JPH01273578A JP H01273578 A JPH01273578 A JP H01273578A JP 63101926 A JP63101926 A JP 63101926A JP 10192688 A JP10192688 A JP 10192688A JP H01273578 A JPH01273578 A JP H01273578A
- Authority
- JP
- Japan
- Prior art keywords
- group
- filter
- container
- filtration
- cylinders
- 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
- 238000001914 filtration Methods 0.000 title claims abstract description 34
- 239000007788 liquid Substances 0.000 claims abstract description 20
- 239000000463 material Substances 0.000 abstract description 14
- 230000008021 deposition Effects 0.000 abstract 1
- 238000000034 method Methods 0.000 description 9
- 238000010586 diagram Methods 0.000 description 4
- 239000012530 fluid Substances 0.000 description 3
- 238000009423 ventilation Methods 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- 238000005273 aeration Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012466 permeate Substances 0.000 description 2
- 241000588724 Escherichia coli Species 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- 210000004102 animal cell Anatomy 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000011001 backwashing Methods 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000010412 perfusion Effects 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004114 suspension culture Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2201/00—Details relating to filtering apparatus
- B01D2201/04—Supports for the filtering elements
- B01D2201/0469—Filter tubes connected to collector tubes
Landscapes
- Filtration Of Liquid (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の目的〕
(産業上の利用分野)
本発明は、連続培養器における?濾過方法およびその装
置に関する。[Detailed Description of the Invention] [Object of the Invention] (Field of Industrial Application) The present invention is directed to continuous culture vessels. The present invention relates to a filtration method and device.
(従来の技術)
従来、高濃度培養器やバイオリアクタにおいては、培養
液循環法あるいは潅流法が用いられ、これらにおいては
各種の膜ン濾過、多孔質ン戸材によるか過、あるいは遠
心分離によっている。(Prior art) Conventionally, culture solution circulation methods or perfusion methods have been used in high-concentration culture vessels and bioreactors, and in these methods, various membrane filtration methods, filtration through porous membrane materials, or centrifugation are used. There is.
しかるに上記のうち前二者は炉材の目詰りの問題があり
、また後者は機構上の複雑さを伴ない、サニテーション
の問題、およびエネルギに関する経費上の問題がある。However, the former two methods have the problem of clogging of the furnace material, and the latter method involves mechanical complexity, sanitation problems, and energy cost problems.
そこでこれらに代るものとして、炉材を用いながら目詰
りが少なく、長期間連続運転が可能な濾過方法として第
5図に示すクロスフロ一方式と称されるものがある。Therefore, as an alternative to these methods, there is a filtration method called the cross-flow one-type method shown in FIG. 5, which uses furnace material, has less clogging, and can be operated continuously for a long period of time.
このクロスフロ一方式は、筒状の炉材aの内部に一端か
ら他端に被濾過液をポンプbの吐出圧によって強制循環
させ、i戸材a内を通る間に炉材aの外周面に透過させ
て濾過する構成である。In this cross-flow one type, the liquid to be filtered is forced to circulate inside a cylindrical furnace material a from one end to the other end by the discharge pressure of a pump b, and while it passes through the inside of the door material a, it is applied to the outer peripheral surface of the furnace material a. It has a configuration that allows it to pass through and filter it.
(発明が解決しようとする課題)
しかしながら上記クロスフロ一方式によっても、炉材a
内の内周面にどうしても浮遊物が付着してしまうため、
圧力損失が経時的に変化し、この圧力損失に伴なう最適
運転条件の設定および濾過面積の決定が極めて困難とな
るという問題があった。(Problem to be Solved by the Invention) However, even with the above-mentioned cross-flow one-way system, the furnace material a
Because floating objects inevitably adhere to the inner circumferential surface of the
There has been a problem in that the pressure loss changes over time, making it extremely difficult to set optimal operating conditions and determine the filtration area due to this pressure loss.
本発明はこれに鑑み、炉材を用いる濾過方式でありなが
らン戸材の目詰りを防止し、長期にわたる連続運転を可
能とする連続培養器におけるン濾過方法およびその装置
を提供することを目的としてなされたものである。In view of this, it is an object of the present invention to provide a method and device for filtration in a continuous culture vessel that prevents clogging of the door material and enables continuous operation over a long period of time, even though it is a filtration method that uses furnace material. This was done as a.
(課題を解決するための手段)
上記従来技術が有する課題を解決するため、本発明は、
容器内に少くとも2本の濾過筒を懸吊支持し、この濾過
筒の外端と容器の下部とを容器外の循環流路により連通
し、この容器内の液を濾過筒の外表面から内部に透過し
て液の少くとも一部または全部を強制循環する間に浮遊
物を濾過筒の外表面で不透過するものであって、前記複
数本の濾過筒を1乃至複数本ずつ1グループとして少く
とも2グループに分け、これら各グループの濾過筒の出
口側を交互に開閉して使用し、一つのグループの濾過筒
が目詰りを起す圧力損失を生じる前にそのグループの濾
過筒を閉止して他側のグループの濾過筒を開らき、この
グループの濾過筒によりン濾過時に生じる容器内の液の
流動により前記閉止したグループの濾過筒の外表面に付
着した浮遊物を剥離させることを特徴とする連続培養器
におけるン濾過方法と、容器と、この容器の天板から容
器内に懸吊支持された複数本の濾過筒と、これら濾過筒
の出口側に接続された流出管と、容器外に設けられ前記
各流出管を合流して前記容器の下部に連なる循環流路と
、前記流出管に設けられた開閉弁とを備え、前記複数本
の濾過筒の1乃至複数本を1グループとしてその開閉弁
をグループ毎に交互に開閉し得るようにしたことを特徴
とする連続培養器における濾過装置とを提供するにある
。(Means for Solving the Problems) In order to solve the problems of the above-mentioned prior art, the present invention provides the following:
At least two filter tubes are suspended and supported in the container, and the outer ends of the filter tubes and the lower part of the container are communicated with each other through a circulation flow path outside the container, so that the liquid in the container is drained from the outer surface of the filter tube. A device that prevents suspended matter from permeating through the outer surface of the filter cylinder while forcing at least part or all of the liquid to pass through the inside, and one or more of the plurality of filter cylinders are included in each group. The filter cylinders of each group are divided into at least two groups, and the outlet sides of the filter cylinders of each group are opened and closed alternately, and the filter cylinders of one group are closed before a pressure loss occurs that causes clogging of the filter cylinders of that group. The filter cylinders of the other group are then opened, and the floating matter adhering to the outer surface of the filter cylinders of the closed group is peeled off by the flow of liquid in the container that occurs during filtration by the filter cylinders of this group. A filtration method in a continuous culture vessel characterized by a container, a plurality of filtration cylinders suspended and supported within the container from the top plate of the container, and an outflow pipe connected to the outlet side of these filtration cylinders, A circulation channel provided outside the container and connecting the respective outflow pipes to a lower part of the container, and an on-off valve provided in the outflow pipe, and one or more of the plurality of filter cylinders are connected to one another. To provide a filtration device for a continuous incubator, characterized in that the on-off valves can be opened and closed alternately for each group.
(作 用)
一方の開閉弁を開らき、他方の開閉弁を閉じて液を循環
させると、この液の流れにより容器内の液は開となって
いる開閉弁側のグループの濾過筒の外表面から濾過筒の
内部へ透過し、これにより濾過が行なわれる。この濾過
筒の外表面に付着した付着物がその外表面全域に至らぬ
前に他側の開閉弁を開け、開らいていた開閉弁を閉じる
と、今度は液が開らいた濾過筒によってン濾過され、運
転を停止した側の濾過筒の外表面に付着していた付着物
は運転を開始した側の濾過筒の外表面へ徐々に移動して
剥離が起る。このように各グループの濾過筒を交互に運
転することによって濾過筒の目詰りが防止されながら連
続運転が可能となる。(Function) When one on-off valve is opened and the other on-off valve is closed to circulate the liquid, this liquid flow causes the liquid in the container to flow out of the filtration cylinder of the group on the open on-off valve side. It permeates from the surface into the inside of the filter cylinder, thereby performing filtration. When the on-off valve on the other side is opened before the deposits attached to the outer surface of the filter tube reach the entire outer surface, and the open on-off valve is closed, the liquid is transferred through the open filter tube. After filtration, the deposits adhering to the outer surface of the filter cylinder on the side where the operation was stopped gradually move to the outer surface of the filter cylinder on the side where the operation was started, and peeling occurs. By operating the filter cylinders of each group alternately in this manner, continuous operation is possible while preventing clogging of the filter cylinders.
(実施例) 以下、本発明を図面に示す実施例を参照して説明する。(Example) The present invention will be described below with reference to embodiments shown in the drawings.
第1図において符号1は、培養器あるいはりアクタ等の
容器であって、一般に浮遊培養、完全混合槽型リアクタ
として用いられ、マイクロキャリヤ等の付着担体を使用
するものであってもよい。In FIG. 1, reference numeral 1 denotes a container such as an incubator or a reactor, which is generally used as a suspension culture or a complete mixing tank type reactor, and may also use an attached carrier such as a microcarrier.
この容器1の上部開口部に固定具2により封着されてい
る天板3に複数本(第1図においては2本)の濾過筒4
0,4□が天板3を貫通して懸吊支持されている。この
濾過筒4□、42の材料としては、フィルム、焼結金属
、セラミックが用いられ、浮遊物の種類に応じてその材
質が選択される。A plurality of (two in FIG. 1) filter cylinders 4 are attached to a top plate 3 that is sealed to the upper opening of the container 1 by a fixture 2.
0.4□ penetrates the top plate 3 and is suspended and supported. Film, sintered metal, or ceramic is used as the material for the filter tubes 4□, 42, and the material is selected depending on the type of suspended matter.
例えば平均孔径が、一般細菌の場合で0. 3〜1.0
μ、酵母大腸菌の場合で0.8〜3μ、動物細胞で15
0〜500μ、植物細胞で0.5〜3”/ 程度とさ
れる。また濾過面積当りの流用
量は0.1〜0.5尻/ −1−(0,6〜3ρ/
ゴh
。7□。)が適当である。For example, the average pore size of common bacteria is 0. 3-1.0
μ, 0.8 to 3 μ for yeast E. coli, 15 for animal cells
0 to 500 μ, and approximately 0.5 to 3”/ for plant cells. Also, the flow rate per filtration area is 0.1 to 0.5 μ/−1−(0.6 to 3 μ/
Goh. 7□. ) is appropriate.
これら濾過筒4..42は2つのグループに分けられ、
各濾過筒4□、4□の外端には流出管50,5゜が接続
され、これら流出管5□、5゜は合流して循環流路6に
接続されており、上記流出管50,52には手動または
自動で開閉される開閉弁70,7□が介挿されている。These filter cylinders4. .. 42 were divided into two groups,
Outflow pipes 50, 5° are connected to the outer ends of each of the filter cylinders 4□, 4□, and these outflow pipes 5□, 5° merge and are connected to the circulation flow path 6. Opening/closing valves 70, 7□, which can be opened and closed manually or automatically, are inserted in 52.
なお図示の実施例では2本の濾過筒4□、4゜を有する
最小単位の場合であるから、一つのグループとして濾過
筒が1本であるが、第2図に略示するように4本の濾過
筒40,4□、43.44を有する場合には2本の濾過
筒44,43を−グループとし、他の濾過筒42.44
を1グループとしてこれら同一グループの濾過筒4□、
43または4 4 の流出管50,53,5゜、542
゛4
を途中で合流させ、この合流後に開閉弁7、。In the illustrated embodiment, the minimum unit has two filter cylinders 4□ and 4°, so there is one filter cylinder in one group, but four filter cylinders are used as shown schematically in Fig. 2. If the filter cylinders 40, 4□, 43.44 are provided, the two filter cylinders 44, 43 are grouped as - group, and the other filter cylinders 42, 44
As one group, these same group of filter cylinders 4□,
43 or 4 4 outflow pipe 50, 53, 5°, 542
``4'' are merged on the way, and after this merge, the on-off valve 7.
72を1グループに1個宛設けるようにすればよい。72 may be provided for one group.
前記循環流路6の途中には、循環駆動源としてのポンプ
8と通気装置9が接続されており、循環流路6の末端は
容器1の下部に接続されていて、濾過された液を容器1
の下部内へ循環させるようになっている。A pump 8 and an aeration device 9 as a circulation drive source are connected in the middle of the circulation flow path 6, and the end of the circulation flow path 6 is connected to the lower part of the container 1, and the filtered liquid is transferred to the container. 1
It is designed to circulate into the lower part of the tank.
前記通気装置9は、前記循環流路6の一部を構成する管
路10の周面に多数の通気孔11..11・・・が開口
され、この通気孔1.1.11・・・の存在する範囲の
管路10を気密に囲続するケーシング12に通気管13
が接続されていて、この通気管13を通じてケーシング
12内に空気を供給することにより前記通気孔11.1
1・・・から液中に空気(酸素)を供給することができ
るようになされている。The ventilation device 9 has a large number of ventilation holes 11. .. 11... are opened, and a vent pipe 13 is installed in a casing 12 that airtightly surrounds the pipe line 10 in the range where the vent holes 1,1,11... exist.
is connected to the vent hole 11.1 by supplying air into the casing 12 through the vent pipe 13.
Air (oxygen) can be supplied into the liquid from 1....
なお前記循環駆動源としては、前記ポンプ8によるほか
、第3図に示すようにインジェクタ14を用いたもので
あってもよい。すなわち循環流路6の途中にインジェク
タ14が接続され、このインジェクタ14の上流側に圧
力流体(例えば空気)を圧送するノズル15を設置し、
このノズル15から噴出する圧力流体により液を圧送す
るようにすることができる。In addition to the pump 8, an injector 14 may be used as the circulation drive source as shown in FIG. 3. That is, an injector 14 is connected in the middle of the circulation channel 6, and a nozzle 15 for feeding pressure fluid (for example, air) is installed upstream of this injector 14.
The liquid can be pumped by pressure fluid ejected from the nozzle 15.
第1図において符号16は給排気系のフィルタを示し、
17は浮遊物を示す。In FIG. 1, reference numeral 16 indicates a filter for the air supply and exhaust system,
17 indicates floating matter.
次に上記実施例の作用を説明する。Next, the operation of the above embodiment will be explained.
いま、開閉弁7 を開、開閉弁7゜を閉とし、ポンプ8
を駆動することにより容器1内の液は流出管54、循環
流路6および途中の通気装置9を経て容器1の下部内へ
循環される。この循環流により容器1内の液は前記間と
なっている開閉弁7 側のグループの濾過筒41の外表
面から濾過筒4、の内部へ透過してポンプ8側へ吸込ま
れてゆく。この間に濾過筒4、の外表面に浮遊物17が
次第に付着する。Now, open the on-off valve 7, close the on-off valve 7°, and turn on the pump 8.
By driving the , the liquid in the container 1 is circulated into the lower part of the container 1 via the outflow pipe 54, the circulation channel 6, and the aeration device 9 in the middle. Due to this circulating flow, the liquid in the container 1 permeates from the outer surface of the filtration cylinder 41 of the group on the on-off valve 7 side, into the inside of the filtration cylinder 4, and is sucked into the pump 8 side. During this time, suspended matter 17 gradually adheres to the outer surface of the filter cylinder 4.
この付着物が濾過筒4□の外表面全域に及ばぬ前に他側
の開閉弁72を開け、開らいていた開閉弁7、を閉じる
ようにすると、今度は液が濾過筒4 の外表面から濾過
筒4゜の内部に透過されてポンプ8へ吸込まれる。Before this deposit does not reach the entire outer surface of the filter cylinder 4, open the on-off valve 72 on the other side and close the on-off valve 7, which was open. The water passes through the filter cylinder 4° and is sucked into the pump 8.
このとき運転を停止した側の濾過筒4□の外表面に付着
した浮遊物17は運転を開始した側の濾過筒4゜の外表
面へ徐々に剥離しつ\移動し、また濾過筒4□の下端か
ら下方へ剥落する。At this time, the suspended matter 17 adhering to the outer surface of the filter tube 4□ on the side where the operation was stopped gradually peels off and moves to the outer surface of the filter tube 4゜ on the side where the operation is started, and the filter tube 4□ It flakes off downward from the bottom edge.
そしてこの濾過筒4゜の外表面に再び浮遊物17が付着
し、この外表面全域に付着が及ぶ前に開閉弁7゜を閉じ
、前述の開閉弁7□を再開して再び前記の濾過筒4□を
用いて運転を継続する。Then, the floating matter 17 adheres to the outer surface of this filter cylinder 4° again, and before the adhesion spreads over the entire outer surface, the on-off valve 7° is closed, the above-mentioned on-off valve 7□ is restarted, and the above-mentioned filter cylinder is removed again. Continue operation using 4□.
これにより濾過筒4□が浮遊物17の付着による目詰り
を起すことが防止され、連続運転を可能とする。This prevents the filter cylinder 4□ from clogging due to adhesion of floating matter 17, and allows continuous operation.
上記開閉弁70,7゜の切換え時期は、液の粘性や菌等
の生体数、その大きさ、粘着性、増殖速度等によって異
なりはするが、これらを勘案してタイマにより切換え時
期を設定することにより自動的に行なうことができる。The switching timing of the above-mentioned on-off valves 70, 7° varies depending on the viscosity of the liquid, the number of living organisms such as bacteria, their size, stickiness, growth rate, etc., but the switching timing is set by a timer taking these into consideration. This can be done automatically.
第4図は濾過筒44,4□への付着物を逆洗により完全
剥離させる機構を付加する場合の一例を略示するもので
、前記流出管5□、5□に逆洗管18 18 を接続し
、この逆洗管18、。FIG. 4 schematically shows an example in which a mechanism is added to completely remove deposits from the filter cylinders 44, 4□ by backwashing, and backwash pipes 18 18 are connected to the outflow pipes 5□, 5□. Connect this backwash pipe 18,.
1′2
18 中の逆洗弁19,192を随時開けることにより
濾過筒40,4゜の内部に圧力流体を供給し、その外表
面に付着する浮遊物17を強制的に剥離させるようにす
ることができる。1'2 18 By opening the backwash valves 19, 192 at any time, pressure fluid is supplied to the inside of the filter cylinder 40, 4°, and the floating matter 17 adhering to the outer surface thereof is forcibly peeled off. be able to.
図示の実施例では、濾過筒の本数が全部で2本の場合と
4本の場合について説明したが、この本数に制限を受け
るものではなく、浮遊物17の種類や性状によって最適
する本数を選択することがてき、また全部の本数が偶数
でなく奇数であってもよい。さらに図示実施例では循環
流路6により完全に閉じられた循環系を示したが、要は
連続的に液を供給して7戸遇するものであれば、本発明
の技術的範囲に含まれることはもちろんである。In the illustrated embodiment, the case where the number of filter cylinders is two in total and the case where there are four in total have been explained, but this number is not limited, and the optimal number is selected depending on the type and properties of the suspended matter 17. Also, the total number may be an odd number instead of an even number. Further, although the illustrated embodiment shows a circulation system completely closed by the circulation channel 6, any system that continuously supplies liquid and serves seven households is within the technical scope of the present invention. Of course.
以上説明したように本発明の濾過方法によれば、一つの
グループの濾過筒の外表面が浮遊物の付着により目詰り
を起す前に他方のグループの濾過筒に切換え、この濾過
筒による濾過時に前記濾過筒の外表面に付着した浮遊物
を剥離させるので、運転を中断させることなくか過を継
続することができ、安定して長期連続運転を行なうこと
ができる。As explained above, according to the filtration method of the present invention, before the outer surface of the filter cylinders of one group becomes clogged due to adhesion of suspended matter, the filter cylinders of the other group are switched to the filter cylinders of the other group, and during filtration with this filter cylinder, Since floating substances adhering to the outer surface of the filter tube are peeled off, filtration can be continued without interrupting operation, and stable continuous operation can be performed for a long period of time.
また本発明の?濾過装置によれば、各グループの濾過筒
の開閉弁の開閉を切換えるのみで各グループの濾過筒を
交互に使用することができ、その開閉操作も開閉弁を電
磁弁とすることにより自動的に行なうことが容易である
などの優れた効果がある。Also of the present invention? According to the filtration device, the filtration cylinders of each group can be used alternately by simply switching the opening and closing of the on-off valves of the filtration cylinders of each group, and the opening and closing operations are automatically performed by using solenoid valves as the on-off valves. It has excellent effects such as being easy to perform.
第1図は本発明の一実施例を示す構成図、第2図は同変
形例を示ず濾過筒存在部分における略示水平断面相当図
、第3図は第1図におけるポンプの代替手段の例示図、
第4図は第1図の実施例に逆洗弁を設けた場合の説明図
、第5図は従来技術を示す説明図である。
1・・・容器、3・・・天板、4□、4゜、4..44
・・・濾過筒、5□、5゜、 53. 54・・・流
出管、6・・・循環流路、7..72・・・開閉弁、8
・・・ポンプ、9・・・通気装置。
出願人代理人 佐 藤 −雄
第1図FIG. 1 is a configuration diagram showing one embodiment of the present invention, FIG. 2 is a schematic horizontal cross-sectional view of the portion where the filter cylinder exists without showing a modification of the same, and FIG. 3 is an alternative means of the pump in FIG. 1. illustrative diagram,
FIG. 4 is an explanatory diagram of a case where a backwash valve is provided in the embodiment of FIG. 1, and FIG. 5 is an explanatory diagram showing a conventional technique. 1... Container, 3... Top plate, 4□, 4°, 4. .. 44
...filter cylinder, 5□, 5°, 53. 54... Outflow pipe, 6... Circulation channel, 7. .. 72...Opening/closing valve, 8
... Pump, 9... Ventilation device. Applicant's agent Mr. Sato Figure 1
Claims (1)
濾過筒の外端と容器の下部とを容器外の循環流路により
連通し、この容器内の液を濾過筒の外表面から内部に透
過して液の少くとも一部または全部を強制循環する間に
浮遊物を濾過筒の外表面で不透過とするものであって、
前記複数本の濾過筒を1乃至複数本ずつを1グループと
して少くとも2グループに分け、これら各グループの濾
過筒の出口側を交互に開閉して使用し、一つのグループ
の濾過筒が目詰りを起す圧力損失を生じる前にそのグル
ープの濾過筒を閉止して他側のグループの濾過筒を開ら
き、このグループの濾過筒により濾過時に生じる容器内
の液の流動により前記閉止したグループの濾過筒の外表
面に付着した浮遊物を剥離させることを特徴とする連続
培養器における濾過方法。 2、容器と、この容器の天板から容器内に懸吊支持され
た複数本の濾過筒と、これら濾過筒の出口側に接続され
た流出管と、容器外に設けられ前記各流出管を合流して
前記容器の下部に連なる循環流路と、前記流出管に設け
られた開閉弁とを備え、前記複数本の濾過筒の1乃至複
数本を1グループとしてその開閉弁をグループ毎に交互
に開閉し得るようにしたことを特徴とする連続培養器に
おける濾過装置。[Claims] 1. At least two filter cylinders are suspended and supported in a container, and the outer ends of the filter cylinders and the lower part of the container are communicated by a circulation channel outside the container. The liquid is permeated from the outer surface of the filter cylinder to the inside, and while at least part or all of the liquid is forcibly circulated, suspended matter is made impermeable on the outer surface of the filter cylinder,
The plurality of filter cylinders are divided into at least two groups, with one or more filter cylinders in each group, and the outlet sides of the filter cylinders in each group are alternately opened and closed, and the filter cylinders in one group are used to prevent clogging. Before a pressure loss occurs that causes a pressure loss, the filtration cylinders of that group are closed and the filtration cylinders of the other group are opened, and the filtration cylinders of this group filter the closed group by the flow of liquid in the container that occurs during filtration. A filtration method in a continuous culture vessel characterized by peeling off suspended matter adhering to the outer surface of a cylinder. 2. A container, a plurality of filtration tubes suspended from the top plate of the container into the container, outflow tubes connected to the outlet side of these filtration tubes, and each of the outflow tubes provided outside the container. It is equipped with a circulation flow path that merges and continues to the lower part of the container, and an on-off valve provided in the outflow pipe, and one or more of the plurality of filter cylinders are set as one group, and the on-off valves are alternately set for each group. A filtration device for a continuous incubator, characterized in that it can be opened and closed at different times.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63101926A JPH01273578A (en) | 1988-04-25 | 1988-04-25 | Filtration method in continuous culture device and apparatus therefor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63101926A JPH01273578A (en) | 1988-04-25 | 1988-04-25 | Filtration method in continuous culture device and apparatus therefor |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01273578A true JPH01273578A (en) | 1989-11-01 |
JPH0371106B2 JPH0371106B2 (en) | 1991-11-12 |
Family
ID=14313519
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63101926A Granted JPH01273578A (en) | 1988-04-25 | 1988-04-25 | Filtration method in continuous culture device and apparatus therefor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01273578A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2609446A (en) * | 2021-07-30 | 2023-02-08 | Oribiotech Ltd | Bioreactor interface plate |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57194015A (en) * | 1981-05-12 | 1982-11-29 | Chemap Ag | Continuous concentration of suspension |
-
1988
- 1988-04-25 JP JP63101926A patent/JPH01273578A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57194015A (en) * | 1981-05-12 | 1982-11-29 | Chemap Ag | Continuous concentration of suspension |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2609446A (en) * | 2021-07-30 | 2023-02-08 | Oribiotech Ltd | Bioreactor interface plate |
Also Published As
Publication number | Publication date |
---|---|
JPH0371106B2 (en) | 1991-11-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US5766949A (en) | Method and apparatus for cultivating anchorage dependent monolayer cells | |
EP0640124B1 (en) | Variable volume reactor-type device and process for the culture of cellular material | |
JP3446399B2 (en) | Immersion type membrane separation device and membrane separation method using the same | |
EP0112155A2 (en) | A method and system for culturing and treating substances disposed in a flowing culture fluid | |
CZ300382B6 (en) | Method for cleaning or protecting membrane modules from siltation | |
JP2777385B2 (en) | Biological cell culture method, culture system and culture device | |
JPH0226626A (en) | Method of preventing and decomposing filter cover layer when liquid containing component distributing finely is filtered by dc/ac operation and apparatus and filter module for implementing the same | |
EP0095804B1 (en) | Process and apparatus for cultivating tissue cells | |
CN107899427A (en) | A kind of MBR membrane stacks on-line cleaning system and cleaning method | |
US4636473A (en) | Membrane and static mixer-moderated bioreactor with anti-fouling device | |
JPH07116482A (en) | Submerged type membrane separation device | |
JPH01273578A (en) | Filtration method in continuous culture device and apparatus therefor | |
JP2007222063A (en) | Culture apparatus and method | |
AU650361B2 (en) | Process and device for filtering liquids | |
CN207786357U (en) | A kind of MBR membrane stacks on-line cleaning system | |
JP6618708B2 (en) | Method for operating hollow fiber membrane module and filtration device | |
CN207418411U (en) | A kind of household reverse osmosis purifier | |
JPS615774A (en) | Apparatus for germ-free collection of fermentation liquor from fermenter | |
CN214880520U (en) | Contact oxidation sewage treatment device | |
JP2500043Y2 (en) | Cell culture device | |
JPH0437935B2 (en) | ||
JP3095464B2 (en) | Cell culture device | |
JPH022895A (en) | Waste water treating device | |
JP2500181B2 (en) | Backwashing method for ceramic membrane | |
CN218089567U (en) | About culture solution treatment facility in microbial incubator |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20071112 Year of fee payment: 16 |
|
S111 | Request for change of ownership or part of ownership |
Free format text: JAPANESE INTERMEDIATE CODE: R313111 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20071112 Year of fee payment: 16 |
|
R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20081112 Year of fee payment: 17 |
|
EXPY | Cancellation because of completion of term | ||
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20081112 Year of fee payment: 17 |