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JPH0615154A - Bubbling device - Google Patents

Bubbling device

Info

Publication number
JPH0615154A
JPH0615154A JP18742091A JP18742091A JPH0615154A JP H0615154 A JPH0615154 A JP H0615154A JP 18742091 A JP18742091 A JP 18742091A JP 18742091 A JP18742091 A JP 18742091A JP H0615154 A JPH0615154 A JP H0615154A
Authority
JP
Japan
Prior art keywords
bubbles
bubble
gas
liquid
air
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP18742091A
Other languages
Japanese (ja)
Inventor
Isao Tamura
伊佐雄 田村
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP18742091A priority Critical patent/JPH0615154A/en
Publication of JPH0615154A publication Critical patent/JPH0615154A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M29/00Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/06Nozzles; Sprayers; Spargers; Diffusers

Landscapes

  • Wood Science & Technology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Health & Medical Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical & Material Sciences (AREA)
  • Zoology (AREA)
  • Biomedical Technology (AREA)
  • Sustainable Development (AREA)
  • Microbiology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Biotechnology (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Abstract

PURPOSE:To provide the bubbling device which can efficiently dissolve and absorb released bubbles into a preserving liquid and can dissolve and absorb the bubbles uniformly over the entire part of the preserving liquid. CONSTITUTION:This bubbling device has a gas release surface 12 for releasing the gas supplied from the outside in a fine bubble form into the liquid. This gas release surface 12 is formed of porous ceramics 9a to 9d having numerous fine continuous open cells.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、例えば細胞保存液中に
酸素等の気体を気泡状にして供給するための泡出し器に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a bubble generator for supplying a gas such as oxygen into a cell preservation solution in the form of bubbles.

【0002】[0002]

【従来の技術】生理学の分野では、生体の細胞を顕微鏡
等で観察して分析する細胞分析が重要な地位を占めてい
る。この細胞分析を行うためには、生体から細胞を含む
塊(組織)を採取し、例えばロータースライサー等によ
って細胞を含む薄切片を作る必要がある。採取された組
織は薄切片にするまで保存容器内の保存液中に漬けて保
存される。保存液内で細胞を活きたままに保存するため
には、適量の酸素(O2)と炭酸ガス(CO2)とを保存液中
に溶解させ、生体中で細胞が生存していたのと同じよう
な環境を作ることが必要である。
2. Description of the Related Art In the field of physiology, cell analysis for observing and analyzing living cells with a microscope or the like occupies an important position. In order to carry out this cell analysis, it is necessary to collect a cell-containing mass (tissue) from a living body and prepare a thin section containing the cells by, for example, a rotor slicer. The collected tissue is immersed and preserved in a preservation solution in a preservation container until it is sliced. In order to keep cells alive in the preservation solution, appropriate amounts of oxygen (O 2 ) and carbon dioxide (CO 2 ) were dissolved in the preservation solution, and the cells survived in the living body. It is necessary to create a similar environment.

【0003】このため、従来では、例えば図1に示すよ
うに、保存液101を収容する容器102内の底部に1
ないし2個の泡出し器(バブラーとも言う)103を沈
め、外部から給気管104を介して酸素と炭酸ガスとの
混合気を各泡出し器103に供給し、泡出し器103の
表面105から気泡として保存液101中に放出するよ
うにしている。
For this reason, conventionally, as shown in FIG. 1, for example, a container 1 containing a storage solution 101 has a bottom portion 1
Or two bubblers (also referred to as bubblers) 103 are submerged, and a mixture of oxygen and carbon dioxide gas is supplied to each bubbler 103 from the outside through the air supply pipe 104, and the surface 105 of the bubbler 103 is supplied. The bubbles are discharged into the storage solution 101.

【0004】各泡出し器103は多孔処理をしたガラス
ボールからなるが、これに代えて、例えば図2に示すよ
うに、多数のピンホール106を形成したゴム管からな
る泡出し器107を用いる場合もある。
Each bubble generator 103 is made of a glass ball that has been subjected to a porous treatment, but instead of this, a bubble generator 107 made of a rubber tube having a large number of pinholes 106 is used as shown in FIG. In some cases.

【0005】[0005]

【発明が解決しようとする課題】ところが、多孔処理に
よりガラスボールに形成される連続気孔や、ピンホール
106は比較的孔径が大きいので、放出される気泡が比
較的大粒になる。例えばガラスボールからなる泡出し器
103の場合には気泡の平均径が1〜数mm程度になり、
ゴム管からなる泡出し器107の場合には気泡の平均径
が0.1〜2mm程度になる。このため、混合気が保存液
101に効率良く溶解ないし吸収されず、混合気の供給
量が多くなり、ランニングコストが高くなるという欠点
がある。
However, since the continuous pores formed in the glass ball by the porosity treatment and the pinhole 106 have a relatively large diameter, the bubbles to be discharged become relatively large. For example, in the case of the bubble generator 103 made of a glass ball, the average diameter of bubbles is about 1 to several mm,
In the case of the bubble generator 107 made of a rubber tube, the average diameter of bubbles is about 0.1 to 2 mm. Therefore, there is a drawback that the air-fuel mixture is not efficiently dissolved or absorbed in the storage liquid 101, the amount of air-fuel mixture supplied increases, and the running cost increases.

【0006】また、ガラスボールからなる泡出し器10
3の場合には気泡を放出する気孔がその表面に局限され
るので、その周囲に気泡が拡散し難く、混合気を保存液
101全体に平均して溶解させ、あるいは、吸収させる
ことが困難になる。ピンホールを有するゴム管からなる
泡出し器107の場合には、泡出し器107を容器10
2の底に沿って馬蹄状、渦巻き状等に配置することによ
り、ピンホール106を容器102の横断面に対して平
均的に分布させることができ、気泡を保存液101中に
より広範囲に分散して供給することができる。
A bubble generator 10 made of a glass ball is also provided.
In the case of 3, since the pores for discharging bubbles are limited to the surface thereof, it is difficult for the bubbles to diffuse around the pores, and it becomes difficult to dissolve or absorb the air-fuel mixture in the entire preservation liquid 101 on average. Become. In the case of the bubble generator 107 made of a rubber tube having a pinhole, the bubble generator 107 is attached to the container 10
By arranging in a horseshoe shape, a spiral shape or the like along the bottom of 2, the pinholes 106 can be distributed evenly with respect to the cross section of the container 102, and the bubbles can be dispersed in a wider range in the preservation liquid 101. Can be supplied.

【0007】しかしながら、この場合でもピンホール1
06の分布密度は制作上一定以上に密にすることができ
ず、気泡をできるだけ平均的に放出するという観点から
は未だに不満が残されている。本発明は、上記の事情を
鑑みてなされたものであり、放出された気泡を効率良く
保存液に溶解ないし吸収させるとともに、保存液全体に
わたりより均一に気泡を溶解ないし吸収させることがで
きる泡出し器を提供することを目的とする。
However, even in this case, the pinhole 1
The distribution density of 06 cannot be made higher than a certain level in production, and dissatisfaction still remains from the viewpoint of discharging bubbles as uniformly as possible. The present invention has been made in view of the above circumstances, and is a foaming device capable of efficiently dissolving or absorbing released bubbles in a preservative solution and more uniformly dissolving or absorbing the bubbles throughout the preservative solution. The purpose is to provide a container.

【0008】[0008]

【課題を解決するための手段】本発明に係る泡出し器
は、上記の目的を達成するため、外部から供給される気
体を液体中に微細泡状にして放出する気体放出面を備
え、この気体放出面が無数の微細連続気孔を有する多孔
質セラミックスで形成されることを特徴とする。
In order to achieve the above-mentioned object, a bubble extractor according to the present invention comprises a gas discharge surface for discharging gas supplied from the outside into a liquid in the form of fine bubbles. It is characterized in that the gas emission surface is formed of a porous ceramic having numerous continuous micropores.

【0009】[0009]

【作 用】多孔質セラミックスは平均孔径が20μm程
度以下の微細連続気孔を無数に備えているので、これを
通して気体を保存液中に放出すれば、その気体は30〜
40μm程度の非常に微細な気泡となって保存液中に放
出される。また、多孔質セラミックスの微細連続気孔の
分布密度は気孔率が例えば30〜40%と非常に高いの
で、気泡が多孔質セラミックスの表面全体にわたって平
均して放出されることになる。
[Operation] Porous ceramics have an infinite number of fine continuous pores with an average pore size of about 20 μm or less.
Very small bubbles of about 40 μm are released into the storage solution. Moreover, since the distribution density of the fine continuous pores of the porous ceramics is very high, for example, 30 to 40%, the bubbles are discharged on average over the entire surface of the porous ceramics.

【0010】[0010]

【実施例】以下、本発明の実施例を図面に基づき具体的
に説明する。図1は本発明の一実施例を備える細胞保存
装置の概略構成図であり、この細胞保存装置は、例えば
市販の酸素ボンベからなる酸素供給源1から供給される
酸素(O2)と、例えば市販の炭酸ガスボンベからなる炭
酸ガス供給源2から供給される炭酸ガス(CO2)とをガス
ミキサ3で混合し、ポンプ4で加圧し、フィルタ5で主
として固形物からなる不純物を除去し、更に、殺菌装置
6で殺菌してから、保存液7を貯留する容器8内の泡出
し器9に供給するように構成されている。
Embodiments of the present invention will be specifically described below with reference to the drawings. FIG. 1 is a schematic configuration diagram of a cell storage device according to an embodiment of the present invention. The cell storage device includes, for example, oxygen (O 2 ) supplied from an oxygen supply source 1 composed of a commercially available oxygen cylinder, and Carbon dioxide gas (CO 2 ) supplied from a carbon dioxide gas supply source 2 composed of a commercially available carbon dioxide gas cylinder is mixed by a gas mixer 3, pressurized by a pump 4, and impurities mainly composed of solid matter are removed by a filter 5, and further, After being sterilized by the sterilization device 6, the preservative solution 7 is supplied to the foaming device 9 in the container 8.

【0011】ガスミキサ3は2種以上(ここでは2種)
の気体を所定の混合比で混合できるように構成してあれ
ばよく、ここでは、人の脳細胞の生存条件に対応して、
酸素と炭酸ガスとを体積比で95:5の割合で混合する
ように構成される。ポンプ4は必要に応じて設けられ、
酸素と炭酸ガスとの混合気を0.1kg/cm2〜1kg/cm2
圧力で吐出するように構成されるが、上記混合気の供給
圧が十分に高い場合にはポンプ4を省略してもよい。
There are two or more kinds of gas mixers 3 (two kinds here).
It suffices if it is configured so that the gas of can be mixed at a predetermined mixing ratio. Here, in order to correspond to the survival condition of human brain cells,
Oxygen and carbon dioxide are mixed at a volume ratio of 95: 5. The pump 4 is provided as needed,
Comprised a mixture of oxygen and carbon dioxide to discharge at a pressure of 0.1kg / cm 2 ~1kg / cm 2 is omitted pump 4 when the supply pressure of the gas mixture is sufficiently high May be.

【0012】後述する泡出し気9に供給される混合気の
圧力が0.1kg/cm2を下回る場合には混合気の保存液7
中への供給量困難になり、供給量が不足するおそれがあ
るので好ましくない。また、泡出し気9に供給される混
合気の圧力が1kg/cm2を上回る場合には、供給量が過剰
になり、気泡の径が大きく成長し過ぎるので好ましくな
い。
When the pressure of the air-fuel mixture supplied to the bubble generation air 9 described later is less than 0.1 kg / cm 2 , the preservative solution 7 for the air-fuel mixture is used.
It is not preferable because the supply amount to the inside becomes difficult and the supply amount may be insufficient. Further, if the pressure of the air-fuel mixture supplied to the bubble-exhaust gas 9 exceeds 1 kg / cm 2 , the supply amount becomes excessive, and the diameter of the bubble grows too large, which is not preferable.

【0013】フィルタ5は、主として固形物からなる不
純物を除去できるように構成してあればよく、水、油等
の濾過液中を気体が通過する湿式フィルタであっても、
濾紙、スポンジ、セラミックス等の多孔体を気体が通過
する乾式フィルタであってもよい。しかし、フィルタ5
は、必要に応じて設けられたものであり、省略すること
が可能である。
The filter 5 only needs to be constructed so as to be able to remove impurities mainly composed of solid matter, and may be a wet filter in which gas passes through a filtrate such as water or oil.
It may be a dry filter in which gas passes through a porous body such as filter paper, sponge, or ceramics. But filter 5
Are provided as needed and can be omitted.

【0014】殺菌装置6は、上記混合気に含まれた細
菌、微生物等を殺菌ないし滅菌できるように構成してあ
ればよく、例えば紫外線等の殺菌ないし滅菌作用を有す
る光線を利用したり、殺菌作用を有する薬剤を利用した
りするものが考えられる。保存液7は、細胞の保存に適
する液体であれば特に限定されず、例えば生理食塩水、
純水、あるいはこれらに抗生物質、栄養源、殺菌剤、抗
菌剤等の細胞の保存に有益な薬剤、細胞の保存に有益な
バクテリア等の微生物等の中の一種あるいは2種以上を
添加した液が使用される。
The sterilizer 6 may be constructed so as to sterilize or sterilize the bacteria, microorganisms, etc. contained in the mixture, for example, using light rays having a sterilizing or sterilizing action such as ultraviolet rays, or sterilizing. It may be possible to use a drug having an action. The storage solution 7 is not particularly limited as long as it is a liquid suitable for storing cells, and for example, physiological saline solution,
Pure water, or a liquid obtained by adding one or more of such agents as antibiotics, nutrients, bactericides, antibacterial agents, etc., which are beneficial for cell preservation, and microorganisms such as bacteria, etc., which are beneficial for cell preservation. Is used.

【0015】容器8は、例えばステンレススチール、ガ
ラス、化学的に安定な合成樹脂等、細胞の保存に無害
で、保存液7の性質を変化させない素材で作られる。ま
た、容器8の形状は細胞塊の出し入れが容易な形状であ
ればよく、例えばここでは有底筒状に形成されている。
上記泡出し器9は本発明の一実施例に係るものであっ
て、図4に示すように四辺形枠状に連結された4本の多
孔質セラミックス管9a〜9dと、その中の1本に形成
した接続孔9eに一端部を挿入して固定された例えばガ
ラス管からなる継手10とを備える。
The container 8 is made of a material, such as stainless steel, glass, and chemically stable synthetic resin, which is harmless to the preservation of cells and does not change the properties of the preservation solution 7. The container 8 may have any shape as long as the cell mass can be easily taken in and out. For example, the container 8 has a bottomed cylindrical shape.
The foaming device 9 according to one embodiment of the present invention includes four porous ceramic tubes 9a to 9d connected in a quadrilateral frame shape as shown in FIG. 4 and one of them. And a joint 10 made of, for example, a glass tube, which is fixed by inserting one end into the connection hole 9e formed in.

【0016】各多孔質セラミックス管9a〜9dの組成
は、特に限定されないが、焼結後に内部に平均孔径が
0.1μmないし20μm程度以下の連続気孔が形成さ
れるような組成が好ましい。連続気孔の平均孔径が20
μm程度を上回ると、放出される気泡の径が40μm程
度を上回り、保存液7に溶解したり、吸収されたりし難
くなるので、好ましくない。また、連続気孔の平均孔径
が0.1μm程度を下回ると通気抵抗が大きくなり過ぎ
るので好ましくない。
The composition of each of the porous ceramics tubes 9a to 9d is not particularly limited, but it is preferable that the composition is such that after sintering, continuous pores having an average pore diameter of 0.1 μm to 20 μm or less are formed inside. The average pore size of continuous pores is 20
If it exceeds about μm, the diameter of the bubbles to be released exceeds about 40 μm, and it becomes difficult for the bubbles to be dissolved or absorbed in the storage liquid 7, which is not preferable. Further, if the average pore diameter of the continuous pores is less than about 0.1 μm, the ventilation resistance becomes too large, which is not preferable.

【0017】この実施例では、ノリタケカンパニーリミ
テド製で、アルミナ(Al2O3)を90重量%含有するセラ
ミックス素材(商品名FS−90)を焼結して得たセラ
ミックスで各多孔質セラミックス管9a〜9dが構成さ
れ、気孔率は30〜45%、嵩比重は2.5〜3.0、
平均気孔径は3〜20μmである。各多孔質セラミック
ス管9a〜9dの両端面は、その中心軸心に対して互い
に反対方向に45°傾斜するように形成されて接着剤で
互いに接着され、継手10は、接続孔9eに接着剤で接
着されるとともに、ゴムホース11を介して殺菌装置6
に接続される。そして、各多孔質セラミックス管9a〜
9dの全表面が気泡放出面12を構成する。
In this embodiment, each porous ceramic tube is made of Noritake Co., Ltd. and is a ceramic obtained by sintering a ceramic material (trade name FS-90) containing 90% by weight of alumina (Al 2 O 3 ). 9a to 9d, the porosity is 30 to 45%, the bulk specific gravity is 2.5 to 3.0,
The average pore diameter is 3 to 20 μm. Both end surfaces of each of the porous ceramic tubes 9a to 9d are formed so as to be inclined at 45 ° in mutually opposite directions with respect to the center axis thereof and are bonded to each other with an adhesive, and the joint 10 is attached to the connection hole 9e with an adhesive. And the sterilizer 6 through the rubber hose 11
Connected to. And each porous ceramics tube 9a-
The entire surface of 9d constitutes the bubble emitting surface 12.

【0018】この細胞保存装置では、泡出し気9の気泡
放出面12に平均気孔径3〜20μmの気孔が気孔率3
0〜45%の高密度に分布しているので、0.1kg/cm2
〜1kg/cm2の圧力で上記混合気を泡出し気9に供給する
と、30〜40μm程度の径の気泡が気泡放出面12全
体にわたって均一に放出される。この気泡は肉眼では観
察できず、透過光の屈折率の変化から保存液7の透明度
が気泡がある部分で低下することを観察することによっ
てその存在を確認できる。そして、保存液7の液面に泡
が発生しないことから、気泡が完全に保存液7に溶解な
いし吸収されたことが分かる。
In this cell storage device, pores having an average pore diameter of 3 to 20 μm are formed on the air bubble emitting surface 12 of the air bubble 9 having a porosity of 3%.
Since it is distributed in a high density of 0 to 45%, 0.1 kg / cm 2
When the air-fuel mixture is supplied to the air bubble 9 at a pressure of ˜1 kg / cm 2 , air bubbles having a diameter of about 30 to 40 μm are uniformly discharged over the entire bubble discharge surface 12. The bubbles cannot be observed with the naked eye, and the presence of the bubbles can be confirmed by observing that the transparency of the preservative solution 7 decreases in the portion where the bubbles are present due to the change in the refractive index of transmitted light. Since no bubbles are generated on the liquid surface of the preservative liquid 7, it can be seen that the bubbles are completely dissolved or absorbed in the preservative liquid 7.

【0019】上記の実施例では、泡出し器9が四辺形枠
状に形成れているが、泡出し器9の形状は特に限定され
ず、例えば三角形枠状、六角形枠状等の多角形枠状、円
環枠状、楕円環枠状、渦巻き管状、馬蹄形管状等に形成
したり、図5に示すようにマット状に形成したり、図6
に示すように偏平な箱状に形成してもよい。図5に示す
本発明の他の実施例では、焼結時に燃焼して消尽する可
燃性中子を使用して、マット状のセラミックスからなる
泡出し器19内に櫛歯状の分岐通気路19aと、この分
岐通気路19aを外部に連通させる幹通気路19bとを
形成している。
In the above-mentioned embodiment, the bubble blower 9 is formed in a quadrilateral frame shape, but the shape of the bubble blower 9 is not particularly limited, and for example, a polygonal shape such as a triangular frame shape or a hexagonal frame shape. It may be formed in a frame shape, an annular frame shape, an elliptic ring frame shape, a spiral tube shape, a horseshoe shape tube shape, or a mat shape as shown in FIG.
It may be formed in a flat box shape as shown in FIG. In another embodiment of the present invention shown in FIG. 5, a combustible core that burns and is exhausted at the time of sintering is used, and a comb-shaped branch air passage 19a is provided in a foamer 19 made of mat-like ceramics. And a trunk ventilation path 19b for communicating the branch ventilation path 19a with the outside.

【0020】この泡出し器19では、主として上側面が
気泡放出面12となる。この泡だし器19のその他の構
成は上記の一実施例の泡出し器9と同様であり、水平面
方向により広範囲にわたって気泡を平均的に放出できる
ことを除けば、その作用及び効果は上記の一実施例と同
様であるので、前例と共通する説明は重複を避けるため
に省略する。
In the bubble dispenser 19, the upper side surface mainly serves as the bubble discharge surface 12. The other configurations of the bubble blower 19 are the same as those of the bubble blower 9 of the above-described embodiment, and the action and effect thereof are the same as those of the above-described one except that the bubbles can be uniformly discharged over a wide range in the horizontal direction. Since it is similar to the example, description common to the previous example is omitted to avoid duplication.

【0021】図6に示す、本発明のまた他の実施例で
は、泡出し器29が身29aと蓋29bとからなる偏平
な箱状に形成される。身29aは例えば、ステンレスス
チール、ガラス、化学的に安定な合成樹脂等、細胞の保
存に無害で、保存液7の性質を変化させない無孔の素材
で作られる。また、蓋29bは上記の各多孔質セラミッ
クス管9a〜9dと同等のセラミックスで作られてい
る。これら身29aと蓋29bとの間に形成される空間
29cは継手29cを介して供給された混合気の動圧を
減衰させる作用を有し、これにより、蓋29aの全面か
ら均等な圧力で気泡が放出されるようになる。
In still another embodiment of the present invention shown in FIG. 6, the foaming device 29 is formed in a flat box shape including a body 29a and a lid 29b. The body 29a is made of a non-porous material, such as stainless steel, glass, and chemically stable synthetic resin, which is harmless to the preservation of cells and does not change the properties of the preservation solution 7. The lid 29b is made of the same ceramic as that of the porous ceramic tubes 9a to 9d. The space 29c formed between the body 29a and the lid 29b has a function of attenuating the dynamic pressure of the air-fuel mixture supplied via the joint 29c, whereby bubbles are uniformly applied from the entire surface of the lid 29a. Will be released.

【0022】この実施例のその他の構成、作用及び効果
は上記各例と同様であるので、これらの説明は重複をさ
けるために省略する。
Other constitutions, operations and effects of this embodiment are the same as those of the above-mentioned respective examples, and therefore their explanations are omitted to avoid duplication.

【0023】[0023]

【発明の効果】以上のように、本発明の泡出し器は、気
泡放出面が多孔質セラミックスで構成されているので、
30〜40μm程度の径の気泡を気泡放出面全体にわた
って平均して放出することができ、効率良く気泡を保存
液に溶解ないし吸収させることができるとともに、保存
液に平均して気泡を溶解ないし吸収させることができ、
混合気の成分ガスの無駄使を無くしてランニングコスト
を安価にできる。
As described above, since the bubble discharge surface of the bubble extractor of the present invention is made of porous ceramics,
Bubbles having a diameter of about 30 to 40 μm can be uniformly discharged over the entire bubble discharge surface, and the bubbles can be efficiently dissolved or absorbed in the storage solution, and the bubbles can be dissolved or absorbed in the storage solution on average. Can be
The running cost can be reduced by eliminating waste of the component gas of the air-fuel mixture.

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

【図1】従来例を備える細胞保存装置の要部の構成図で
ある。
FIG. 1 is a configuration diagram of a main part of a cell storage device including a conventional example.

【図2】他の従来例の斜視図である。FIG. 2 is a perspective view of another conventional example.

【図3】本発明の一実施例を備える細胞保存装置の構成
図である。
FIG. 3 is a configuration diagram of a cell storage device according to an embodiment of the present invention.

【図4】本発明の一実施例の斜視図である。FIG. 4 is a perspective view of an embodiment of the present invention.

【図5】本発明の他の実施例の斜視図である。FIG. 5 is a perspective view of another embodiment of the present invention.

【図6】本発明のまた他の実施例の斜視図である。FIG. 6 is a perspective view of another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

7 保存液 9 泡出し器 9a 多孔質セラミックス管 9b 多孔質セラミックス管 9c 多孔質セラミックス管 9d 多孔質セラミックス管 12 気泡放出面 19 泡出し器 29 泡出し器 29b 蓋 7 Preservative Liquid 9 Foamer 9a Porous Ceramics Tube 9b Porous Ceramics Tube 9c Porous Ceramics Tube 9d Porous Ceramics Tube 12 Bubble Ejecting Surface 19 Foamer 29 Foamer 29b Lid

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 外部から供給される気体を液体中に微細
泡状にして放出する気体放出面を備え、この気体放出面
が無数の微細連続気孔を有する多孔質セラミックスで形
成されることを特徴とする泡出し器。
1. A gas discharge surface for discharging a gas supplied from the outside into a liquid in the form of fine bubbles, and the gas discharge surface is formed of a porous ceramic having innumerable fine continuous pores. A whisk.
【請求項2】 微細連続気孔の平均孔径が20μm程度
以下である請求項1に記載の泡出し器。
2. The bubble generator according to claim 1, wherein the average pore diameter of the fine continuous pores is about 20 μm or less.
JP18742091A 1991-07-26 1991-07-26 Bubbling device Pending JPH0615154A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18742091A JPH0615154A (en) 1991-07-26 1991-07-26 Bubbling device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18742091A JPH0615154A (en) 1991-07-26 1991-07-26 Bubbling device

Publications (1)

Publication Number Publication Date
JPH0615154A true JPH0615154A (en) 1994-01-25

Family

ID=16205738

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18742091A Pending JPH0615154A (en) 1991-07-26 1991-07-26 Bubbling device

Country Status (1)

Country Link
JP (1) JPH0615154A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09168792A (en) * 1995-12-19 1997-06-30 Mitsumasa Murakami Fine bubble forming apparatus
JP2003071260A (en) * 2001-06-22 2003-03-11 Ngk Insulators Ltd Apparatus for manufacturing aqueous carbonic acid solution and water-cleaning system provided with the same
WO2005056168A1 (en) * 2003-12-15 2005-06-23 Miyazaki Prefecture Method of forming monodisperse bubble
JP2006052427A (en) * 2004-08-10 2006-02-23 Nuclear Fuel Ind Ltd Device for generating methyltrichlorosilane gas
JP2009269026A (en) * 2008-05-07 2009-11-19 Mctech Co Ltd Module for dissolution of gas
JP2022511113A (en) * 2018-12-11 2022-01-28 アプライド マテリアルズ インコーポレイテッド Ampoule splash reduction

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09168792A (en) * 1995-12-19 1997-06-30 Mitsumasa Murakami Fine bubble forming apparatus
JP2003071260A (en) * 2001-06-22 2003-03-11 Ngk Insulators Ltd Apparatus for manufacturing aqueous carbonic acid solution and water-cleaning system provided with the same
WO2005056168A1 (en) * 2003-12-15 2005-06-23 Miyazaki Prefecture Method of forming monodisperse bubble
JP2006052427A (en) * 2004-08-10 2006-02-23 Nuclear Fuel Ind Ltd Device for generating methyltrichlorosilane gas
JP2009269026A (en) * 2008-05-07 2009-11-19 Mctech Co Ltd Module for dissolution of gas
JP2022511113A (en) * 2018-12-11 2022-01-28 アプライド マテリアルズ インコーポレイテッド Ampoule splash reduction

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