JP2922202B1 - Liquid solvent separation method and apparatus in microorganism culturing apparatus - Google Patents

Liquid solvent separation method and apparatus in microorganism culturing apparatus

Info

Publication number
JP2922202B1
JP2922202B1 JP21177698A JP21177698A JP2922202B1 JP 2922202 B1 JP2922202 B1 JP 2922202B1 JP 21177698 A JP21177698 A JP 21177698A JP 21177698 A JP21177698 A JP 21177698A JP 2922202 B1 JP2922202 B1 JP 2922202B1
Authority
JP
Japan
Prior art keywords
separation membrane
microorganism
liquid solvent
culture solution
porous filtration
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.)
Expired - Fee Related
Application number
JP21177698A
Other languages
Japanese (ja)
Other versions
JP2000023658A (en
Inventor
高広 鈴木
行雄 坂庭
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.)
JIO SAHOOTO JUGEN
Original Assignee
JIO SAHOOTO JUGEN
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 JIO SAHOOTO JUGEN filed Critical JIO SAHOOTO JUGEN
Priority to JP21177698A priority Critical patent/JP2922202B1/en
Application granted granted Critical
Publication of JP2922202B1 publication Critical patent/JP2922202B1/en
Publication of JP2000023658A publication Critical patent/JP2000023658A/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Apparatus Associated With Microorganisms And Enzymes (AREA)

Abstract

【要約】 【課題】 多孔質濾過分離膜を用いることによって微生
物培養液中の液体溶媒を効率よく分離回収する。 【解決手段】 培養容器1上方の気相空間7に多孔質濾
過分離膜9を多数配置するとともに培養容器1下方に造
波用の翼板10を配置し,この翼板10を往復回動する
ことによって培養容器1に収容した微生物培養液8を遥
動して,これを気相空間7の多孔質濾過分離膜9に強制
接触させ,強制接触の衝撃で目詰り物質を洗浄してその
目詰りを防止しながら,分離膜9の毛管現象により微生
物培養液8から液体溶媒を分離回収する。
Abstract: PROBLEM TO BE SOLVED: To efficiently separate and collect a liquid solvent in a microorganism culture solution by using a porous filtration separation membrane. SOLUTION: A number of porous filtration / separation membranes 9 are arranged in a gas phase space 7 above a culture vessel 1, and a wave-making blade 10 is arranged below the culture vessel 1, and the blade 10 is reciprocated. As a result, the microbial culture solution 8 contained in the culture vessel 1 is swung to force the microbial culture solution 8 into contact with the porous filtration / separation membrane 9 in the gas phase space 7, and the clogged substance is washed by the impact of the forced contact to remove the eye. While preventing clogging, the liquid solvent is separated and recovered from the microorganism culture solution 8 by capillary action of the separation membrane 9.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は微生物培養装置に関
し,特に培養容器における微生物培養液から液体溶媒を
分離する微生物培養装置における液体溶媒分離方法及び
装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a microorganism culturing apparatus, and more particularly to a method and apparatus for separating a liquid solvent in a microorganism culturing apparatus for separating a liquid solvent from a microorganism culture solution in a culture vessel.

【0002】[0002]

【発明が解決しようとする課題】多孔質濾過分離膜を用
いることにより培養容器における微生物培養液から液体
溶媒を分離する方法及び装置は,本発明者中の一方の発
明者により,例えば特開平5−95778号,特開平6
−98758号等をもって提案済であるが,これらは,
多孔質濾過分離膜を隔膜として配置し,例えば通気によ
る圧力差によって,微生物培養液中の液体溶媒を通過さ
せ,その分離回収を行なうものとされるため,微生物培
養液における分離膜を物理的に通過し得ない固形微粒子
や不溶性粉末等が目詰り物質となり,これが多孔質濾過
分離膜の目詰り原因となり,これに起因した濾過流量の
低下を招くことにより,良好な濾過効率を維持し得ない
可能性を残している。
A method and an apparatus for separating a liquid solvent from a microorganism culture solution in a culture vessel by using a porous filtration separation membrane have been disclosed by one of the present inventors, for example, in Japanese Patent Laid-Open No. No. 95778, JP-A-6
−98758, etc.
A porous filtration membrane is arranged as a membrane, and the liquid solvent in the microbial culture is passed through, for example, by a pressure difference due to aeration, and the separation and recovery are performed. Solid fine particles and insoluble powders that cannot pass through become clogging substances, which cause clogging of the porous filtration separation membrane, thereby resulting in a decrease in filtration flow rate and failing to maintain good filtration efficiency. The possibility remains.

【0003】上記目詰りとこれによる濾過流量低下を防
止するため,例えば間欠的に或いは必要に応じて非培養
液側からの逆洗浄を行なう逆洗浄装置を設置したり,微
生物培養液にケイ藻土等の濾過助剤を添加したりする等
の措置を採ることが可能であるが,この場合濾過のため
の設備費が高価になったり,ランニングコストが掛かっ
たりするとともにその操作や添加作業を必要として管理
が煩雑化することにもなる一方,これらも結局目詰りに
対して抜本的な対策をなすものではないから,この種培
養装置において多孔質濾過分離膜の濾過とこれに伴う目
詰りの関係を解消して,濾過効率を良好に維持すること
が望まれる。
[0003] In order to prevent the clogging and a reduction in the filtration flow rate due to the clogging, for example, a backwashing device for performing backwashing intermittently or as necessary from the non-culture solution side is installed, or diatoms are added to the microorganism culture solution. It is possible to take measures such as adding a filter aid such as soil. However, in this case, the equipment cost for filtration is high, the running cost is high, and the operation and addition work are required. Although it is necessary to complicate the management, these methods also do not provide a drastic measure against clogging. Therefore, in this seed culture apparatus, filtration of the porous filtration separation membrane and clogging accompanying the filtration are performed. It is desired to eliminate the relationship and maintain good filtration efficiency.

【0004】本発明は,かかる事情に鑑みてなされたも
ので,その解決課題とするところは,多孔質濾過分離膜
の濾過を可及的良好に行なうとともに該濾過に伴う目詰
りを解消して,濾過効率を可及的良好に維持し得るよう
にした微生物培養装置における液体溶媒分離方法及び装
置を提供するにある。
[0004] The present invention has been made in view of the above circumstances, and an object of the present invention is to perform filtration of a porous filtration membrane as efficiently as possible and to eliminate clogging accompanying the filtration. Another object of the present invention is to provide a method and an apparatus for separating a liquid solvent in a microorganism culturing apparatus capable of maintaining filtration efficiency as good as possible.

【0005】[0005]

【課題を解決するための手段】上記課題に添って本発明
者らは,鋭意研究を重ねた結果,上記多孔質濾過分離膜
として,例えば特開平5−95778号に示されるよう
に,多孔質セラミック膜,多孔質ガラス膜,多孔質有機
高分子膜,金属繊維編織体,金属焼結体等を使用可能で
あるところ,これら分離膜は,液体溶媒分離のためのフ
ィルター作用を果たすものであるが,これらは,それぞ
れそれ自体液体に対して毛管現象(毛細管現象)を呈す
るものである点に着目し,微生物培養液を収容する培養
容器上方に気相空間を形成するとともに該気相空間に多
孔質濾過分離膜を配置し,微生物培養液をこの気相空間
の多孔質濾過分離膜に対して強制的に接触させることに
よって,上記多孔質濾過分離膜の毛管現象により微生物
培養液中から液体溶媒を吸収通過させ,微生物培養液の
濾過を良好に行なうことが可能になるとともに,このと
き分離膜を通過し得ない微生物培養液中の上記固形微粒
子や不溶性粉末等の目詰り物質が分離膜の表面に付着す
ることがあるが,微生物培養液の強制的な接触により多
孔質濾過分離膜は,表面を接触衝撃を受けながら洗われ
ることになるから,付着した目詰り物質は接触した培養
液とともに微生物培養液中に落下復帰し,分離膜の表面
に付着のままその目詰りの原因となることなく,目詰り
解消のための自然洗浄のサイクルを形成することが可能
となり,微生物培養液の濾過において目詰りを解消し,
濾過効率を高度に維持する上で極めて有効である事実を
見いだした。
Means for Solving the Problems In view of the above problems, the present inventors have conducted intensive studies, and as a result, as described in JP-A-5-95778, for example, as a porous filtration separation membrane, Ceramic membrane, porous glass membrane, porous organic polymer membrane, woven metal fiber, sintered metal, etc. can be used, but these separation membranes act as a filter for liquid solvent separation. However, focusing on the fact that each of them exhibits a capillary phenomenon (capillary phenomenon) with respect to the liquid, a gas phase space is formed above the culture vessel containing the microorganism culture solution, and the gas phase space is formed. A porous filtration separation membrane is arranged, and the microbial culture solution is forcibly brought into contact with the porous filtration separation membrane in the gas-phase space. The medium can be absorbed and passed, and the microorganism culture solution can be filtered well. At this time, clogging substances such as the solid fine particles and insoluble powder in the microorganism culture solution that cannot pass through the separation membrane are removed. May adhere to the surface of the microbe, but the porous filtration membrane is washed while receiving a contact impact on the surface due to the forced contact of the microbial culture medium. At the same time, it falls back into the microbial culture solution and forms a natural washing cycle to eliminate the clogging without adhering to the surface of the separation membrane without causing clogging. Eliminate clogging during filtration,
It has been found that it is extremely effective in maintaining a high filtration efficiency.

【0006】本発明はかかる知見に基づいてなされたも
ので,即ち請求項1に記載の発明は,上記課題のうち液
体溶媒分離方法を提供するように,これを,培養容器内
の上方気相空間に配置した多孔質濾過分離膜に該培養容
器収容の微生物培養液を強制的に接触させ,該微生物培
養液中の液体溶媒を上記多孔質濾過分離膜における毛管
現象の吸収通過によって分離回収することを特徴とする
微生物培養装置における液体溶媒分離方法とし,請求項
2に記載の発明は,上記に加えて,上記多孔質濾過分離
膜による液体溶媒の濾過を促進し,十分な濾過性能を確
保し得るように,これを,上記気相空間の多孔質濾過分
離膜を,中空パイプ状の分離膜としその中空部を継続的
又は間欠的に引圧状態とすることを特徴とする請求項1
に記載の微生物培養装置における液体溶媒分離方法と
し,請求項3に記載の発明は,上記課題のうち液体溶媒
分離装置を提供するように,これを,培養容器と,該培
養容器の上方気相空間に配置した多孔質濾過分離膜と,
該培養容器内収容の微生物培養液を上記気相空間におけ
る多孔質濾過分離膜に強制的に接触させる強制接触手段
とを備えてなることを特徴とする微生物培養装置におけ
る液体溶媒分離装置とし,請求項4及び5に記載の発明
は,上記に加えて,それぞれ多孔質濾過分離装置に対す
る微生物培養液の強制接触を簡易且つ確実に行なって好
ましい強制接触手段とするように,請求項4に記載の発
明を,上記強制接触手段を,培養容器中の微生物培養液
を造波遥動する造波手段によるものとしてなることを特
徴とする請求項1に記載の微生物培養装置における液体
溶媒分離装置とし,請求項5に記載の発明を,上記強制
接触手段を,培養容器中の微生物培養液を気相空間に噴
出又は飛散する飛沫形成手段によるものとしてなること
を特徴とする請求項1に記載の微生物培養装置における
液体溶媒分離装置とし,請求項6に記載の発明は,同じ
く上記に加えて,上記多孔質濾過分離膜による液体溶媒
の濾過を促進し,十分な濾過性能を確保し得るように,
これを,上記多孔質濾過分離膜を,中空パイプ状の分離
膜としその中空部を継続的又は間欠的に引圧状態とする
引圧手段を追加的に備えてなることを特徴とする請求項
3,4又は5に記載の微生物培養装置における液体溶媒
分離装置とし,これらをそれぞれ発明の要旨として上記
課題解決の手段としたものである。
[0006] The present invention has been made based on such knowledge, that is, the present invention according to claim 1 is directed to providing a method for separating a liquid solvent from the above-mentioned problems by using an upper gas phase in a culture vessel. The microbial culture solution contained in the culture container is forcibly brought into contact with the porous filtration separation membrane arranged in the space, and the liquid solvent in the microbial culture solution is separated and recovered by absorption passage of the capillary phenomenon in the porous filtration separation membrane. A method for separating a liquid solvent in a microorganism culturing apparatus, characterized in that, in addition to the above, in addition to the above, the filtration of the liquid solvent by the porous filtration separation membrane is promoted to ensure sufficient filtration performance. 2. The method according to claim 1, wherein the porous filtration separation membrane in the gas phase space is a hollow pipe-shaped separation membrane, and the hollow portion is continuously or intermittently pressurized.
According to a third aspect of the present invention, there is provided a method for separating a liquid solvent in a microbial culture apparatus, comprising the steps of: A porous filtration membrane arranged in a space,
A liquid solvent separation device in a microorganism culture device, comprising: forced contact means for forcibly bringing the microorganism culture solution contained in the culture container into contact with the porous filtration separation membrane in the gas phase space. In addition to the above, the inventions described in Claims 4 and 5 are intended to perform simple and reliable forced contact of the microorganism culture solution with the porous filtration / separation apparatus, thereby providing preferable forced contact means. The invention is characterized in that the forcible contacting means is constituted by wave-making means for wave-forming and oscillating a microorganism culture solution in a culture vessel, wherein the liquid solvent separation device in the microorganism culturing apparatus according to claim 1, The invention according to claim 5 is characterized in that the forcible contact means is constituted by a droplet forming means for ejecting or scattering a microorganism culture solution in a culture vessel into a gas phase space. The liquid solvent separating apparatus in the microorganism culturing apparatus according to the first aspect, wherein the invention according to the sixth aspect further enhances the filtration of the liquid solvent by the porous filtration separation membrane to secure sufficient filtration performance in addition to the above. To be able to
The porous filtration separation membrane is formed as a hollow pipe-shaped separation membrane, and a pressure reducing means for continuously or intermittently reducing the pressure of the hollow portion is further provided. A liquid solvent separating device in the microorganism culturing device described in 3, 4, or 5, which is used as a means for solving the above problem as a gist of the invention.

【0007】[0007]

【発明の実施の形態】以下図面の例に従って本発明を更
に詳しく説明すれば,図1及び図2において,Aは微生
物培養装置,Bはその液体溶媒分離装置を示し,該液体
溶媒分離装置Bは,培養容器1と,該培養容器1の上方
気相空間7に配置した多孔質濾過分離膜9と,該培養容
器1内収容の微生物培養液8を上記気相空間7における
多孔質濾過分離膜9に強制的に接触させる強制接触手段
とを備えたものとしてあり,本例において上記強制接触
手段は,これを,培養容器1中の微生物培養液8を造波
遥動する造波手段によるものとしてある。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in more detail with reference to the drawings. In FIGS. 1 and 2, A denotes a microorganism culturing apparatus, B denotes a liquid solvent separating apparatus, and B denotes a liquid solvent separating apparatus. Is a porous filtration separation membrane 9 arranged in the culture vessel 1, a gas phase space 7 above the culture vessel 1, and a microbial culture solution 8 contained in the culture vessel 1. And a forced contact means for forcibly contacting the membrane 9. In the present embodiment, the forced contact means is provided by a wave forming means for wave-forming and moving the microorganism culture solution 8 in the culture vessel 1. There are things.

【0008】本例にあって培養容器1は,例えば円筒体
の両端に閉塞側板をボルトにより取外し自在に固定し,
液面を上下中間位置,特に中央位置とするように円筒体
の下側半円部を,例えば30乃至100リットル程度の
適宜容量にして微生物培養液8を収容する培養液収容部
とし,上側半円部を該培養液収容部上の気相空間7とし
た,例えばステンレス製横置き用の円筒形のものとして
ある。
In this embodiment, the culture vessel 1 has, for example, detachably fixed closed side plates at both ends of a cylindrical body with bolts.
The lower semicircular portion of the cylindrical body is set to an appropriate volume of, for example, about 30 to 100 liters so as to accommodate the microbial culture solution 8 so that the liquid surface is at the middle position between the upper and lower sides, particularly the center position. The circular portion is a gas-phase space 7 above the culture solution accommodating portion, and is, for example, a stainless-steel horizontal cylinder.

【0009】本例にあって多孔質濾過分離膜9は,中空
パイプ状の分離膜とした,例えば上記各種材料中から膜
孔0.2ミクロンメートル径の多孔質セラミック分離
膜,即ちセラミック多孔質管によるものとし,本例にお
いて該分離膜は,これを気相空間に多数配置し,気相空
間7にあって微生物培養液8の液面上方に離隔してこれ
を覆う如くに配置し,後述の微生物培養液8の強制接触
を可及的効率的に行なうように培養容器1内にその円筒
交差方向にむけて取外し自在に架設してあり,本例の分
離膜9は,これを円筒長手方向のやや離隔した複数位置
に各複数本を近接して平行に並列するとともにこれを上
下に段状とした複数並列複数段のブロック状又は群状の
配置によるものとしてあり,本例にあってこの配置は,
例えば2ヵ所にそれぞれ下側3本,上側2本の各5本を
用いて,上記強制接触の効率性を確保するようにしたも
のとしてある。
In this embodiment, the porous filtration separation membrane 9 is a hollow pipe-shaped separation membrane, for example, a porous ceramic separation membrane having a pore diameter of 0.2 μm from the above various materials, that is, a ceramic porous separation membrane. In this example, the separation membranes are arranged in a gas phase space, and in the gas phase space 7, the separation membranes are arranged so as to be spaced above the liquid surface of the microorganism culture solution 8 so as to cover them. It is detachably mounted in the culture vessel 1 in the direction intersecting the cylinder so as to make the forcible contact of the microorganism culture solution 8 described later as efficiently as possible. In this example, a plurality of pieces are arranged in parallel in parallel in close proximity to a plurality of positions slightly spaced apart from each other in the longitudinal direction, and the pieces are arranged stepwise up and down. Lever arrangement
For example, the efficiency of the above-mentioned forced contact is ensured by using the lower three wires and the upper two wires each at two locations.

【0010】多孔質濾過分離膜9は,それぞれその長手
方向一端に中空部に連通するように接続したチューブ乃
至パイプ3を介して図示省略の濾過液槽に連結してあ
り,このときチューブ乃至パイプ3の長手方向中間に同
じく図示省略のポンプを介設し,該ポンプを引圧手段と
することによって,上記各多孔質濾過分離膜9の中空部
を継続的又は間欠的に引圧状態としてあり,本例の該引
圧状態は,上記ポンプを,例えばチュービングポンプと
することによって,これを間欠的に行なうものとしてあ
る。
The porous filtration / separation membrane 9 is connected to a filtrate tank (not shown) via a tube or pipe 3 connected to one end in the longitudinal direction thereof so as to communicate with the hollow portion. Similarly, a pump (not shown) is interposed in the middle in the longitudinal direction of the filter 3 and the pump is used as a pressure reducing means, whereby the hollow portion of each of the porous filtration separation membranes 9 is continuously or intermittently compressed. In this embodiment, the pressure is reduced intermittently by using a tubing pump, for example.

【0011】本例にあって強制接触手段の造波手段は,
これを培養容器1中にあって微生物培養液8に造波の外
力を付与してこれを遥動することによって,上記気相空
間において多孔質濾過分離膜9に対して微生物培養液8
を強制接触するものとしてあり,本例の該造波手段は,
図示省略のモーターに,例えばクランクを介して偏心固
定することによって往復回動する回動軸11に固定して
微生物培養液8中で往復運動を行なうように配置し,微
生物培養液8を押圧して遥動造波する翼板10によるも
のとしてあり,本例の翼板10は,培養容器1の上記両
端又はその一方の閉塞側板に設置した軸受12に軸支し
該培養容器1の円筒体の中央に位置して上記回動軸11
に固定した,高さ(上下長さ)を円筒体の半径を基準と
して,これよりやや短寸にし,その往復運動により微生
物培養液8の押圧とこれによる遥動造波を有効に行い,
該微生物培養液8の波を培養容器1の円筒の内壁面に添
って上昇落下させて気相空間7に跳ね上げ状とし,上記
多孔質濾過分離膜9に強制接触させるものとしてある。
In this embodiment, the wave forming means of the forced contact means is
This is placed in the culture vessel 1 and imparts a wave-forming external force to the microbial culture 8 to cause it to move, thereby causing the microbial culture 8 to pass through the porous filtration separation membrane 9 in the gas phase space.
Are forcibly contacted with each other.
A motor (not shown) is eccentrically fixed via a crank, for example, and is fixed to a rotating shaft 11 that reciprocates and is arranged so as to reciprocate in the microorganism culture solution 8. The wing plate 10 of this embodiment is supported by bearings 12 installed on both ends or one of the closed side plates of the culture container 1. Of the rotation shaft 11
The height (vertical length) fixed to the base is slightly shorter than the radius of the cylindrical body, and the reciprocating motion effectively presses the microbial culture solution 8 and effectively performs the oscillating wave-making.
The wave of the microorganism culture solution 8 is raised and dropped along the inner wall surface of the cylinder of the culture vessel 1 so as to jump up into the gas phase space 7, and is forced into contact with the porous filtration separation membrane 9.

【0012】このとき本例の造波手段における上記翼板
10は,上記回動軸11に所定角度,例えば60度の角
度をなすように一対を対向状に配置するとともに回動軸
11の回動角度,即ち翼板10の回動角度を所定角度,
例えば60乃至80度程度に設定して,上記翼板10が
微生物培養液8を3区分するようにするとともに培養容
器1の円筒体の内側双方に対して微生物培養液8を遥動
造波するようにして,該翼板10の往復運動に応じてそ
れぞれ逆方向から,培養容器1の円筒体における上記円
筒交差方向の多孔質濾過分離膜9に,その長手方向両側
から微生物培養液8の強制接触を行なうものとしてあ
り,またこのとき上記翼板10は,上記多孔質濾過分離
膜9の配置,特にその上記複数並列複数段のブロック又
は群毎にそれぞれこれらに対する造波手段として,回動
軸11長手方向に並置して設置するものとし,本例にあ
ってこの設置は,上記一対の翼板10を同一の回動軸1
1に対して,その長手方向に並置するように2対4枚用
いて,培養容器1においてその全体に亘る遥動造波を行
なうようにしたものとしてある。
At this time, the wing plate 10 in the wave-making means of the present embodiment is arranged such that a pair thereof is opposed to the rotating shaft 11 so as to form a predetermined angle, for example, an angle of 60 degrees, and the rotating shaft 11 is The moving angle, that is, the turning angle of the blade 10 is a predetermined angle,
For example, the angle is set to about 60 to 80 degrees, so that the wing plate 10 divides the microorganism culture solution 8 into three sections, and the microorganism culture solution 8 is made to wave in both directions inside the cylindrical body of the culture vessel 1. Thus, the microbial culture solution 8 is forcibly applied to the porous filtration / separation membrane 9 in the cross direction of the cylinder in the cylindrical body of the culture vessel 1 from opposite directions in accordance with the reciprocating motion of the wing plate 10. At this time, the wing plate 10 is provided with a rotating shaft as an arrangement of the porous filtration / separation membrane 9, and in particular, as a wave-forming means for each of the plurality of blocks or groups of the plurality of parallel stages. In this embodiment, the pair of wing plates 10 are mounted on the same rotating shaft 1.
In contrast, the culture vessel 1 uses two to four pieces so as to be juxtaposed in the longitudinal direction so as to perform oscillating wave making over the entirety of the culture vessel.

【0013】図中2は,培養容器1の視認窓,4は上記
濾過液槽から図示省略のポンプによって濾過した液体溶
媒を培養容器に循環させるチューブ又はパイプ,5は,
例えば好気性菌の微生物を培養するについてエアを送入
し,炭酸ガスを排出するように培養容器1の気相空間7
における気相管理を行なう吸排孔,6は培養容器1の温
度を調節する温調水循環用のジャケットをそれぞれ示
す。
In the figure, reference numeral 2 denotes a visual window of the culture vessel 1, reference numeral 4 denotes a tube or pipe for circulating a liquid solvent filtered from the filtrate tank by a pump (not shown) to the culture vessel, and reference numeral 5 denotes a pipe.
For example, air is supplied for culturing microorganisms of aerobic bacteria, and the gas phase space 7 of the culture vessel 1 is discharged so as to discharge carbon dioxide gas.
In the figure, reference numeral 6 denotes a suction / discharge hole for performing gas phase management, and reference numeral 6 denotes a jacket for circulating a temperature-regulating water for controlling the temperature of the culture vessel 1.

【0014】以上のように構成した微生物培養装置Aに
おける液体溶媒分離装置Bは,培養容器1の微生物培養
液8から液体溶媒を分離するように用いるものとしてあ
り,これをその液体溶媒分離方法によって説明すれば,
培養容器1内の上方気相空間7に配置した多孔質濾過分
離膜9に該培養容器1収容の微生物培養液8を強制的に
接触させ,該微生物培養液8中の液体溶媒を上記多孔質
濾過分離膜9における毛管現象の吸収通過によって分離
回収するものとし,このとき該分離回収は,本例にあっ
てこれを,上記気相空間7の多孔質濾過分離膜9を,中
空パイプ状の分離膜としその中空部を継続的又は間欠
的,特に間欠的に引圧状態とすることによって行なうも
のとしてある。
The liquid solvent separating device B in the microorganism culturing device A configured as described above is used to separate a liquid solvent from the microorganism culturing solution 8 in the culture vessel 1, and this is separated by the liquid solvent separating method. To explain,
The microbial culture solution 8 contained in the culture container 1 is forcibly brought into contact with a porous filtration separation membrane 9 arranged in the upper gas phase space 7 in the culture container 1, and the liquid solvent in the microbial culture solution 8 is removed from the porous medium. Separation and recovery are performed by absorption and passage of the capillary phenomenon in the filtration and separation membrane 9. In this case, the separation and recovery is performed by replacing the porous filtration and separation membrane 9 in the gas phase space 7 with a hollow pipe-like shape in the present embodiment. The separation is performed by continuously or intermittently, particularly intermittently, applying a pressure to the hollow portion of the separation membrane.

【0015】即ち培養容器1には,円筒体の中心を通る
水平線を液面とするように,培地に微生物と必要に応じ
た添加物を添加混合した微生物培養液8を収容するもの
とし,その液体溶媒の分離は,造波手段を作動,本例に
あってはモーターに通電して回動軸11を回動すること
によって,造波手段の翼板10を往復回動させ微生物培
養液8を遥動造波し,培養容器1の湾曲した内壁面に衝
接し,その誘導により,微生物培養液8を多孔質濾過分
離膜9に落下させて,これに強制接触させ,多孔質濾過
分離膜9の毛管現象により液体溶媒をこれに浸透させて
その中空部に分離するものとしてあり,このとき毛管現
象により浸透した液体溶媒は,重力を受けて中空部に自
然落下することになるが,本例にあっては,上記ポンプ
により多孔質濾過分離膜9の中空部が引圧され,表面に
対して減圧の状態になるので,毛管現象により浸透した
液体溶媒を吸引するように作用して,毛管現象を促進し
て,液体溶媒の分離を確実にして有効に行ない得るよう
にしてある。
That is, the culture vessel 1 contains a microorganism culture solution 8 in which microorganisms and additives are added and mixed in a culture medium such that a horizontal line passing through the center of the cylinder is a liquid surface. In order to separate the liquid solvent, the wave forming means is operated. In this example, the motor is energized and the rotating shaft 11 is rotated, whereby the wing plate 10 of the wave forming means is reciprocated and the microorganism culture solution 8 is rotated. The microbial culture 8 is dropped on the porous filtration / separation membrane 9, and is forced into contact with the porous filtration / separation membrane 9. The liquid solvent permeated by capillary action is separated into the hollow part by the capillary action of No. 9, and the liquid solvent permeated by the capillary action drops naturally into the hollow part due to gravity. In the example, porous filtration by the above pump Since the hollow portion of the separation membrane 9 is depressurized and depressurized against the surface, it acts to suck the liquid solvent that has penetrated by capillary action, promotes the capillary action, and separates the liquid solvent. It is made sure that it can be done effectively.

【0016】一方上記膜孔径との関係で,各種菌等の微
生物は微生物培養液8中に残ることになるが,固形微粒
子,不溶性粉末等の微生物培養液8中の上記目詰り物質
は,上記強制接触により同時に多孔質濾過分離膜9の表
面に接触しこれに付着するが,強制接触によって多孔質
濾過分離膜9に与えられる衝撃によって,表面から微生
物培養液とともに洗い流されて微生物培養液8中に落下
復帰することになり,この自動洗浄の作用が形成される
ことで,目詰り物質が多孔質濾過分離膜9の表面に付着
したまま,その目詰りを招来することが可及的確実に防
止されることになり,その液体溶媒の分離による濾過効
率を極めて良好に維持することが可能となる。
On the other hand, microorganisms such as various bacteria remain in the microorganism culture solution 8 in relation to the membrane pore size. However, the clogging substances in the microorganism culture solution 8 such as solid fine particles and insoluble powder are as described above. The forced contact simultaneously contacts and adheres to the surface of the porous filtration and separation membrane 9, but is washed away from the surface together with the microorganism culture by the impact given to the porous filtration and separation membrane 9 by the forced contact, and As a result, the clogging substance is caused to adhere to the surface of the porous filtration separation membrane 9 as much as possible. Thus, the filtration efficiency by the separation of the liquid solvent can be maintained extremely well.

【0017】微生物培養液8から多孔質濾過分離膜9に
より濾過されて分離された中空部の液体溶媒は,引圧手
段により引かれて上記チューブ又はパイプ3を介して濾
過液槽に回収され,必要な調整を経て,再度微生物培養
液8に戻され,微生物の培養に好適な環境を形成し得る
ようにしてある。
The liquid solvent in the hollow portion, which is separated from the microorganism culture solution 8 by filtration through the porous filtration separation membrane 9, is pulled by the pressure means and collected in the filtrate tank via the tube or pipe 3. After necessary adjustment, it is returned to the microorganism culture solution 8 again so that an environment suitable for culturing microorganisms can be formed.

【0018】図3及び4は,他の例を示すもので,本例
の微生物培養装置Aにおける液体溶媒分離装置Bにあっ
て,培養容器1は横長矩形のボックス状として,同じく
上方を気相空間7とした,例えば同じくステンレス製横
長ボックス形のものとし,多孔質濾過分離膜9は,これ
を気相空間7の液面上方に離隔してこれを覆う如くに,
ボックスの長手方向に向けて取外し自在に架設してあ
り,本例の分離膜9は,これをほぼ面をなすように中央
部をやや離隔した複数の両側位置に各複数本を近接して
平行に並列した複数並列の面群の配置によるものとして
あり,本例にあってこの配置は,例えば両側にそれぞれ
5本を用いて,上記強制接触の効率性を確保するように
したものとしてある。
FIGS. 3 and 4 show another example. In the liquid solvent separator B in the microorganism culturing apparatus A of the present embodiment, the culture vessel 1 is formed in a horizontally-long rectangular box shape, and the upper part is also a gas phase. The space 7 is made of, for example, a horizontally long box made of stainless steel, and the porous filtration separation membrane 9 is separated above the liquid surface of the gas phase space 7 so as to cover it.
The separation membrane 9 of this embodiment is detachably mounted in the longitudinal direction of the box. The separation membrane 9 of the present example is arranged in parallel with a plurality of the separation membranes 9 at a plurality of both side positions slightly separated from the center so that the separation membranes 9 are substantially flat. In this example, for example, five arrangements are used on both sides to ensure the efficiency of the forced contact described above.

【0019】強制接触手段は,本例にあってこれを,培
養容器1中の微生物培養液8を気相空間7に噴出又は飛
散する飛沫形成手段によるものとしてあり,即ち本例の
飛沫形成手段は,培養容器1中又は培養容器1外に設置
した培養液噴出ポンプ13により,培養容器1の対角線
の交点位置から,多孔質濾過分離膜9の離隔したスペー
スを介して気相空間7上方に微生物培養液8を噴出し,
培養容器1の天井面,本例ではこれに設けたディフュー
ザー14に衝接させて,上記面状の多孔質濾過分離膜9
に微生物培養液8を飛沫状に落下させることによって,
その強制接触を行なうようにしたものとしてある。
In the present embodiment, the forced contact means is formed by a spray forming means for ejecting or scattering the microorganism culture solution 8 in the culture vessel 1 into the gas phase space 7, that is, the spray forming means of the present embodiment. Is above the gas phase space 7 from the intersection of the diagonal lines of the culture vessel 1 through the space separated by the porous filtration separation membrane 9 by the culture solution ejection pump 13 installed in the culture vessel 1 or outside the culture vessel 1. Spout the microbial culture 8
The flat porous filtration membrane 9 is brought into contact with the ceiling surface of the culture vessel 1, in this example, the diffuser 14 provided therein.
By dropping the microbial culture solution 8 in the form of droplets,
The forced contact is made.

【0020】その余は上記例のものと基本的に同一の構
成としたので,同一符号を付してその説明を省略する
が,本例にあっては,上記図1及び図2の例において図
示を省略した培養容器1に対する微生物培養液(基質
液)の供給槽15,そのポンプ16,エアコンプレッサ
17,その除菌フィルター18,濾過液槽19,その各
ポンプ20を示したので,上記図1及び図2の例におい
てはこれに準じて微生物培養装置Aを構成するようにす
ればよい。
The rest of the configuration is basically the same as that of the above-mentioned example, so the same reference numerals are given and the explanation is omitted. In this example, however, in the example of FIG. 1 and FIG. The figure shows a supply tank 15, a pump 16, an air compressor 17, a sterilization filter 18, a filtrate tank 19, and a pump 20 thereof for a microorganism culture solution (substrate solution) for the culture vessel 1 not shown. In the examples of FIGS. 1 and 2, the microorganism culturing apparatus A may be configured according to this.

【0021】本例の微生物培養装置Aにおける液体溶媒
分離装置Bにおいても,培養容器1の上下中間位置を通
る水平線を液面とするように,微生物培養液8を収容
し,その液体溶媒の分離は,飛沫形成手段を作動,本例
にあっては培養液噴出ポンプ13を作動して,微生物培
養液8を噴出して,上記飛沫状の落下により多孔質濾過
分離膜9に強制接触させるようにして,同様に引圧状態
で多孔質濾過分離膜9の毛管現象による液体溶媒の分離
回収を行なうとともに飛沫状の落下の強制接触による自
動洗浄の作用によって目詰り物質の多孔質濾過分離膜9
に対する目詰りの招来を同様に防止し,濾過効率を極め
て良好に維持するものとされるに至り,上記の例と同様
な作用効果を呈するものとすることができる。
In the liquid solvent separator B of the microorganism culturing apparatus A of this embodiment, the microorganism culturing solution 8 is also accommodated so that a horizontal line passing through the upper and lower middle positions of the culture vessel 1 is used as the liquid surface, and the liquid solvent is separated. In this example, the droplet forming means is operated, and in this example, the culture solution ejection pump 13 is operated to eject the microorganism culture solution 8 and force the microorganism culture solution 8 into contact with the porous filtration separation membrane 9 by the above-mentioned dropping. Similarly, the liquid solvent is separated and recovered by capillary action of the porous filtration / separation membrane 9 under a reduced pressure state, and the porous filtration / separation membrane 9 for clogged substances is automatically washed by the forced contact of the droplets.
In the same manner, it is possible to prevent the occurrence of clogging, to maintain the filtration efficiency extremely satisfactorily, and to exhibit the same operation and effect as in the above example.

【0022】図示した例は以上のとおりとしたが,多孔
質濾過分離膜は,これを平板状のパネルとし,これをそ
の下位に配置した一体又は別体の受皿とともに用いて,
該受皿に液体溶媒を分離し,受皿を介して濾過液槽等に
回収するようにすること,強制接触手段を用いるとき,
これを培養容器を載置固定する培養容器遥動手段による
ものとし,また培養容器内に設置した水平回転版とこれ
により回転した微生物培養液を上方に誘導落下する衝接
板を備えた回転落下手段によるものとすること,強制接
触手段を造波手段とするとき,微生物培養液の多孔質濾
過分離膜への接触を促進する,ディフューザーを培養容
器の内壁に配置すること,強制接触手段を飛沫形成手段
とするとき,上記ポンプを培養容器外に設置し,チュー
ブ又はパイプにより培養容器の気相空間上方から微生物
培養液を飛沫として飛散する循環系のものとして構成す
ること,引圧手段を用いるとき,多孔質濾過分離膜の中
空部を継続的に引圧するものとすること等を含めて,本
発明の実施に当って,培養容器,その気相空間,多孔質
濾過分離膜,微生物培養液,必要に応じて用いる強制接
触手段,その例の造波手段や飛沫形成手段,引圧手段等
の各具体的材質,形状,構造,寸法,容量,数,大き
さ,用途等は,上記発明の要旨に反しない限り様々に変
更して,適宜の形態のものとすることができる。
Although the illustrated example is as described above, the porous filtration / separation membrane is formed as a flat panel, which is used together with an integral or separate saucer disposed thereunder.
Separating the liquid solvent in the pan and collecting it in the filtrate tank via the pan, when using forced contact means,
This is to be performed by means of a culture vessel swinging means for mounting and fixing the culture vessel, and a horizontal drop plate provided in the culture vessel and a rotary dropper provided with an abutment plate for guiding and dropping the rotated microorganism culture solution upward. When the forced contact means is wave-forming means, it promotes contact of the microbial culture solution with the porous filtration separation membrane, a diffuser is arranged on the inner wall of the culture vessel, and the forced contact means is splashed. When the pump is used as the forming means, the pump is installed outside the culture vessel, and the pump is configured as a circulating system in which the microorganism culture solution is scattered as droplets from above the gas phase space of the culture vessel by a tube or a pipe. In the practice of the present invention, including, for example, continuously reducing the pressure in the hollow portion of the porous filtration separation membrane, the culture vessel, its gas phase space, the porous filtration separation membrane, Specific materials, shapes, structures, dimensions, capacities, numbers, sizes, uses, etc. of the culture solution, forced contact means used as necessary, wave forming means, droplet forming means, and pressure reducing means of the examples are as follows. Various modifications can be made to an appropriate form without departing from the gist of the invention.

【0023】[0023]

【実施例1】図1及び図2の微生物培養装置Aにおける
培養容器1を容量4L用とし,酵母エキス10g/L,
トリプトン30g/L,グリコース5g/Lを含むpH
7の培地2Lに大腸菌を植菌し,37°Cで1日間培養
し,酵母エキス10g/L,トリプトン30g/Lを含
む同じくpH7の基質液を供給して引圧下の濾過分離を
し乍ら培養を行なった。この間翼板10を毎分60回の
サイクルで往復回動して微生物培養液8の多孔質濾過分
離膜9への強制接触を継続して行なったところ,培養3
日目までに菌体濃度50g/Lにして生菌率95%を得
た。このとき濾過流量は当初の90%,希釈率は0.3
-1であり,残存グルコースは全く検出されず,菌体の
分離率は99%であった。
Example 1 A culture vessel 1 in a microorganism culturing apparatus A shown in FIGS. 1 and 2 was used for a capacity of 4 L, and yeast extract 10 g / L,
PH containing 30 g / L of tryptone and 5 g / L of glucose
E. coli was inoculated into 2 L of medium No. 7 and cultured at 37 ° C. for 1 day. A substrate solution of the same pH 7 containing 10 g / L of yeast extract and 30 g / L of tryptone was supplied, and the mixture was separated by filtration under reduced pressure. Culture was performed. During this time, the wing plate 10 was reciprocated at a cycle of 60 times per minute to continuously forcibly contact the microbial culture solution 8 with the porous filtration separation membrane 9.
By the day, the cell concentration was 50 g / L, and a viable cell rate of 95% was obtained. At this time, the filtration flow rate was initially 90%, and the dilution rate was 0.3.
h- 1 , no residual glucose was detected, and the isolation rate of the cells was 99%.

【0024】[0024]

【比較例1】造波手段の翼板10を取外した同じ微生物
培養装置Aを用い,多孔質濾過分離膜9を微生物培養液
8中に浸漬設置し,引圧下の濾過分離をし乍ら同様の培
養を行なった。濾過流量は急速に低下し,培養3日目の
希釈率は0.05h-1となり,菌体濃度15g/Lにし
て生菌率10%であった。
COMPARATIVE EXAMPLE 1 Using the same microorganism culturing apparatus A from which the wing plate 10 of the wave-making means was removed, the porous filtration separation membrane 9 was immersed and installed in the microorganism culture solution 8, and the filtration separation was performed under reduced pressure. Was cultured. The filtration flow rate rapidly decreased, and the dilution ratio on the third day of culture was 0.05 h -1 . The viable cell ratio was 10% when the cell concentration was 15 g / L.

【0025】[0025]

【実施例2】図3及び図4の微生物培養装置Aにおける
培養容器1を容量5L用とし,培養液噴出ポンプ13に
よる微生物培養液8の噴出を毎分3Lとして微生物培養
液8の多孔質濾過分離膜9への強制接触を継続して行な
った以外は,実施例1と同様の条件で培養を行なった。
培養3日目までに菌体濃度60g/Lにして生菌率90
%を得た。このとき濾過流量は同様に当初の90%,希
釈率は0.3h-1であり,残存グルコースは全く検出さ
れず,菌体の分離率は99%であった。
Example 2 Porous filtration of a microorganism culture solution 8 in which the culture vessel 1 in the microorganism culture apparatus A shown in FIGS. 3 and 4 is used for a capacity of 5 L and the ejection of the microorganism culture solution 8 by the culture solution ejection pump 13 is set to 3 L per minute. Culture was performed under the same conditions as in Example 1 except that forced contact with the separation membrane 9 was continued.
By 3 days of culture, the cell concentration was adjusted to 60 g / L, and the viable cell rate was 90%.
%. At this time, the filtration flow rate was similarly 90% at the initial stage, the dilution rate was 0.3 h -1 , no residual glucose was detected, and the bacterial cell separation rate was 99%.

【0026】[0026]

【比較例2】培養液噴出ポンプ13を作動することなく
同じ微生物培養装置Aを用い,多孔質濾過分離膜9を微
生物培養液8中に浸漬設置し,引圧下の濾過分離をし乍
ら同様の培養を行なった。濾過流量は急速に低下し,培
養3日目の希釈率は0.05h-1となり,菌体濃度10
g/Lにして生菌率8%であった。
[Comparative Example 2] Using the same microorganism culturing apparatus A without operating the culture liquid ejection pump 13, the porous filtration / separation membrane 9 was immersed in the microorganism culture liquid 8, and filtered and separated under reduced pressure. Was cultured. The filtration flow rate rapidly decreased, and the dilution rate on the third day of culture was 0.05 h -1 , and the cell concentration was 10 h.
The viable cell ratio was 8% in g / L.

【0027】[0027]

【発明の効果】本発明は以上のとおりに構成したので,
請求項1に記載の発明は,多孔質濾過分離膜の濾過を可
及的良好に行なうとともに該濾過に伴う目詰りを解消し
て,濾過効率を可及的良好に維持し得るようにした微生
物培養装置における液体溶媒分離方法を提供することが
可能になり,請求項2に記載の発明は,上記に加えて,
上記多孔質濾過分離膜による液体溶媒の濾過を促進し,
十分な濾過性能を確保し得るものとすることができ,請
求項3に記載の発明は,多孔質濾過分離膜の濾過を可及
的良好に行なうとともに該濾過に伴う目詰りを解消し
て,濾過効率を可及的良好に維持し得るようにした微生
物培養装置における液体溶媒分離装置を提供することが
可能になり,請求項4及び5に記載の発明は,上記に加
えて,それぞれ多孔質濾過分離装置に対する微生物培養
液の強制接触を簡易且つ確実に行なって好ましい強制接
触手段とすることができ,請求項6に記載の発明は,同
じく上記に加えて,上記多孔質濾過分離膜による液体溶
媒の濾過を促進し,十分な濾過性能を確保し得るものと
することができる。
The present invention is configured as described above.
According to the first aspect of the present invention, there is provided a microorganism capable of performing filtration of a porous filtration separation membrane as satisfactorily as possible, eliminating clogging caused by the filtration, and maintaining filtration efficiency as satisfactorily as possible. It is possible to provide a method for separating a liquid solvent in a culture device, and the invention according to claim 2 provides, in addition to the above,
Promote the filtration of liquid solvent by the porous filtration separation membrane,
A sufficient filtration performance can be ensured, and the invention according to claim 3 performs filtration of the porous filtration separation membrane as satisfactorily as possible and eliminates clogging accompanying the filtration. It is possible to provide a liquid solvent separation device in a microorganism culturing device capable of maintaining the filtration efficiency as good as possible. The forced contact of the microorganism culture solution with the filtration / separation device can be performed easily and reliably as a preferred forced contact means. It is possible to promote the filtration of the solvent and ensure sufficient filtration performance.

【図面の簡単な説明】[Brief description of the drawings]

【図1】培養容器の円筒交差方向中間位置における微生
物培養装置の縦断面図である。
FIG. 1 is a longitudinal sectional view of a microorganism culturing apparatus at an intermediate position of a culture vessel in a direction crossing a cylinder.

【図2】培養容器の前後方向中間位置における微生物培
養装置の縦断面図である。
FIG. 2 is a longitudinal sectional view of the microorganism culturing apparatus at an intermediate position in the front-rear direction of the culture vessel.

【図3】他の例の微生物培養装置の一部を破断した斜視
図である。
FIG. 3 is a partially cutaway perspective view of a microorganism culturing apparatus of another example.

【図4】培養容器の前後方向中間位置における図3の微
生物培養装置の縦断面図である。
4 is a longitudinal sectional view of the microorganism culturing apparatus of FIG. 3 at an intermediate position in the front-rear direction of the culture vessel.

【符号の説明】[Explanation of symbols]

A 微生物培養装置 B 液体溶媒分離装置 1 培養容器 7 気相空間 8 微生物培養液 9 多孔質濾過分離膜 10 翼板 13 噴出ポンプ Reference Signs List A Microorganism culture device B Liquid solvent separation device 1 Culture vessel 7 Gas phase space 8 Microorganism culture solution 9 Porous filtration separation membrane 10 Blade plate 13 Jet pump

───────────────────────────────────────────────────── フロントページの続き (72)発明者 坂庭 行雄 東京都文京区白山1丁目36番2号ライオ ンズマンション文京白山108号 有限会 社ジオサポ−ト内 (56)参考文献 特開 平6−98758(JP,A) 特開 平5−95778(JP,A) 特開 平5−84429(JP,A) (58)調査した分野(Int.Cl.6,DB名) C12M 1/00 - 3/04 B01D 61/00 - 71/82 ──────────────────────────────────────────────────続 き Continuation of the front page (72) Inventor Yukio Sakaba 1-36-2 Hakusan, Bunkyo-ku, Tokyo Lions Mansion Bunkyo Hakusan 108 Within Geo Support Co., Ltd. (56) References JP-A-6-98758 (JP, A) JP-A-5-95778 (JP, A) JP-A-5-84429 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) C12M 1/00-3 / 04 B01D 61/00-71/82

Claims (6)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 培養容器内の上方気相空間に配置した多
孔質濾過分離膜に該培養容器収容の微生物培養液を強制
的に接触させ,該微生物培養液中の液体溶媒を上記多孔
質濾過分離膜における毛管現象の吸収通過によって分離
回収することを特徴とする微生物培養装置における液体
溶媒分離方法。
1. A microbial culture solution contained in a culture container is forcibly brought into contact with a porous filtration separation membrane disposed in an upper gas phase space in a culture container, and the liquid solvent in the microorganism culture solution is subjected to the porous filtration. A method for separating a liquid solvent in a microorganism culturing apparatus, wherein separation and recovery are performed by absorption and passage of capillary action in a separation membrane.
【請求項2】 上記気相空間の多孔質濾過分離膜を,中
空パイプ状の分離膜としその中空部を継続的又は間欠的
に引圧状態とすることを特徴とする請求項1に記載の微
生物培養装置における液体溶媒分離方法。
2. The method according to claim 1, wherein the porous filtration separation membrane in the gas phase space is a hollow pipe-shaped separation membrane, and the hollow portion is continuously or intermittently brought into a pressure-reducing state. A liquid solvent separation method in a microorganism culturing apparatus.
【請求項3】 培養容器と,該培養容器の上方気相空間
に配置した多孔質濾過分離膜と,該培養容器内収容の微
生物培養液を上記気相空間における多孔質濾過分離膜に
強制的に接触させる強制接触手段とを備えてなることを
特徴とする微生物培養装置における液体溶媒分離装置。
3. A culture vessel, a porous filtration separation membrane disposed in a gas phase space above the culture vessel, and a microorganism culture solution contained in the culture vessel being forcibly applied to the porous filtration separation membrane in the gas phase space. A liquid solvent separation device in a microorganism culturing device, comprising: forced contact means for contacting the liquid solvent.
【請求項4】 上記強制接触手段を,培養容器中の微生
物培養液を造波遥動する造波手段によるものとしてなる
ことを特徴とする請求項1に記載の微生物培養装置にお
ける液体溶媒分離装置。
4. The apparatus for separating a liquid solvent in a microorganism culturing apparatus according to claim 1, wherein said forced contact means is constituted by wave-forming means for wave-forming and oscillating a microorganism culture solution in a culture vessel. .
【請求項5】 上記強制接触手段を,培養容器中の微生
物培養液を気相空間に噴出又は飛散する飛沫形成手段に
よるものとしてなることを特徴とする請求項1に記載の
微生物培養装置における液体溶媒分離装置。
5. The liquid in the microorganism culturing apparatus according to claim 1, wherein said forced contact means is formed by a droplet forming means for ejecting or scattering a microorganism culture solution in a culture vessel into a gas phase space. Solvent separator.
【請求項6】 上記多孔質濾過分離膜を,中空パイプ状
の分離膜としその中空部を継続的又は間欠的に引圧状態
とする引圧手段を追加的に備えてなることを特徴とする
請求項3,4又は5に記載の微生物培養装置における液
体溶媒分離装置。
6. The method according to claim 1, wherein the porous filtration separation membrane is formed as a hollow pipe-shaped separation membrane and further provided with a pressure reducing means for continuously or intermittently reducing the pressure of the hollow portion. A liquid solvent separation device in the microorganism culturing device according to claim 3, 4 or 5.
JP21177698A 1998-07-10 1998-07-10 Liquid solvent separation method and apparatus in microorganism culturing apparatus Expired - Fee Related JP2922202B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21177698A JP2922202B1 (en) 1998-07-10 1998-07-10 Liquid solvent separation method and apparatus in microorganism culturing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21177698A JP2922202B1 (en) 1998-07-10 1998-07-10 Liquid solvent separation method and apparatus in microorganism culturing apparatus

Publications (2)

Publication Number Publication Date
JP2922202B1 true JP2922202B1 (en) 1999-07-19
JP2000023658A JP2000023658A (en) 2000-01-25

Family

ID=16611414

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21177698A Expired - Fee Related JP2922202B1 (en) 1998-07-10 1998-07-10 Liquid solvent separation method and apparatus in microorganism culturing apparatus

Country Status (1)

Country Link
JP (1) JP2922202B1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003042352A1 (en) 2001-11-16 2003-05-22 Phytoculture Control Co., Ltd. Apparatus for culturing organism and method of culturing organism

Also Published As

Publication number Publication date
JP2000023658A (en) 2000-01-25

Similar Documents

Publication Publication Date Title
JP3577460B2 (en) Rotating disk type filtration device equipped with means for reducing axial force
US7537696B2 (en) Method and apparatus for treatment of wastewater employing membrane bioreactors
CN102527134B (en) High flow disc filter
EP0086539B1 (en) Device for culturing micro-organisms
DE19905645C1 (en) Filter attachment for vacuum filtration
JP2002512109A (en) Rotary filtration device with flow-through inner member
US20090026139A1 (en) Submerged cross-flow filtration
CN108479122A (en) A kind of defoaming device and the broken wall foam fraction factor purification system containing the device
WO1985002783A1 (en) Filtration method and apparatus
SG184911A1 (en) Membrane unit and membrane separation device
JP2922202B1 (en) Liquid solvent separation method and apparatus in microorganism culturing apparatus
CN214485929U (en) Coating canning is with microfiltration device
CN111252841A (en) Impeller type air-float sewage treatment equipment
CN115786075A (en) A tissue dissociation device
CN114570066A (en) Chemical sewage coalescence-separation equipment
JP2011189308A (en) Active-sludge treatment apparatus and operation method thereof
JP3417455B2 (en) Sludge thickener using filtration membrane
CN222821313U (en) Vibrating flat membrane filter
CN221131872U (en) Pharmaceutical equipment can be used to solution ultrafiltration device
CN223752503U (en) A device for purifying and reusing degreasing waste liquid
JPH0716398B2 (en) Gas-liquid contact method and device
CN219836163U (en) Separation filter equipment is used in production of cascaded peanut goods
CN211998918U (en) An impeller type air flotation sewage treatment equipment
CN110734849A (en) Microalgae harvesting and spray liquid leaching system
US4159950A (en) Filter apparatus

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

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees