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JPS6234436B2 - - Google Patents
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JPS6234436B2 - - Google Patents

Info

Publication number
JPS6234436B2
JPS6234436B2 JP58032890A JP3289083A JPS6234436B2 JP S6234436 B2 JPS6234436 B2 JP S6234436B2 JP 58032890 A JP58032890 A JP 58032890A JP 3289083 A JP3289083 A JP 3289083A JP S6234436 B2 JPS6234436 B2 JP S6234436B2
Authority
JP
Japan
Prior art keywords
gas
liquid
ventilation pipe
impeller
present
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
Application number
JP58032890A
Other languages
Japanese (ja)
Other versions
JPS59160516A (en
Inventor
Tetsusaburo Sato
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 JP58032890A priority Critical patent/JPS59160516A/en
Publication of JPS59160516A publication Critical patent/JPS59160516A/en
Publication of JPS6234436B2 publication Critical patent/JPS6234436B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/233Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
    • B01F23/2331Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements
    • B01F23/23311Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements through a hollow stirrer axis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/233Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
    • B01F23/2331Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/233Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
    • B01F23/2336Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the location of the place of introduction of the gas relative to the stirrer
    • B01F23/23364Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the location of the place of introduction of the gas relative to the stirrer the gas being introduced between the stirrer elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05Stirrers
    • B01F27/11Stirrers characterised by the configuration of the stirrers
    • B01F27/112Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
    • B01F27/1125Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades with vanes or blades extending parallel or oblique to the stirrer axis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05Stirrers
    • B01F27/11Stirrers characterised by the configuration of the stirrers
    • B01F27/13Openwork frame or cage stirrers not provided for in other groups of this subclass

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Gas Separation By Absorption (AREA)

Description

【発明の詳細な説明】 本発明は気液混合装置、更に詳しく言えば液体
に気体を混合させて微粒気泡を発生させる曝気装
置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a gas-liquid mixing device, and more particularly to an aeration device that mixes gas with a liquid to generate fine air bubbles.

従来、此種装置としては水中ポンプで液体を噴
出せしめ、通気孔から送られた気体を強制的に差
込ませて液体中に微粒気泡を発生させる装置があ
るが、水深の深い所では膨大な動力を要するた
め、実質的に2m未満の水深の浅い液中でしか使
用できず、その用途は極めて限られる欠点があつ
た。
Conventionally, this type of device uses a submersible pump to eject liquid and forcefully inserts gas sent through a vent hole to generate microscopic bubbles in the liquid, but in deep water, a huge amount of air bubbles are generated. Since it requires power, it can only be used in shallow liquids of less than 2 m depth, which has the disadvantage that its applications are extremely limited.

従来装置の前記欠点を解消する装置として、第
1図に示すように通気パイプAの下方部に放射状
の隔板を取付け、液体取入口Cから取入れた液体
を液槽中に放射し、この放射流によつて気体噴出
孔Dから噴出する空気を吸引させる装置が提案さ
れている(実公昭52―6955号参照)。しかしなが
らこの装置は確かに水深2m以上の液中でも有効
に機能するが、大規模な曝気には適さず、しかも
液体排出口および気体排出口ともに幅狭く、複雑
な構成になつているため、糸屑その他の屑物によ
り目詰りが起り易く、このため駆動モーターに過
負荷がかかり、モーター寿命を縮めてしまい、し
かし一旦屑物がからまると除去するのが困難で、
再生利用ができない欠点がある。
As a device to solve the above-mentioned drawbacks of the conventional device, as shown in Fig. 1, a radial partition plate is attached to the lower part of the ventilation pipe A, and the liquid taken in from the liquid intake port C is radiated into the liquid tank. A device has been proposed in which the air ejected from the gas outlet D is sucked by the flow (see Utility Model Publication No. 52-6955). However, although this device certainly functions effectively even in liquids at a depth of 2 meters or more, it is not suitable for large-scale aeration, and both the liquid and gas outlets are narrow and have a complicated configuration, so it does not remove lint. Other debris can easily cause clogging, which can overload the drive motor and shorten its lifespan.However, once debris is entangled, it is difficult to remove.
It has the disadvantage that it cannot be recycled.

本発明者は此等従来曝気装置の欠点を解消し、
汎用性が高くしかも取扱いの簡便な装置を得んと
して鋭意研究の結果、液体の過流により生ずる負
圧を利用すればよいことに想到し、本発明を完成
させるに至つた。
The present inventor has solved the drawbacks of these conventional aeration devices,
As a result of intensive research in an effort to obtain a device that is highly versatile and easy to handle, the inventors came up with the idea of utilizing the negative pressure generated by overflow of liquid, and thus completed the present invention.

以下実施例を示す第2図〜第5図により本発明
の内容を説明する。
The content of the present invention will be explained below with reference to FIGS. 2 to 5 showing examples.

即ち、本発明は上方に気体取入口1bを有し且
つ下方側部1cに複数の気体噴出口1dを穿設し
た通気パイプ1と、前記通気パイプ1に沿う様通
気パイプ1の下方側部1cに固定したインペラー
2と、通気パイプ1の下端開口部を閉塞する盲板
3とを有して成る気液混合装置である。
That is, the present invention provides a ventilation pipe 1 having a gas intake port 1b in the upper part and a plurality of gas jet ports 1d in the lower side part 1c, and a lower side part 1c of the ventilation pipe 1 along the ventilation pipe 1. This is a gas-liquid mixing device comprising an impeller 2 fixed to the air and a blind plate 3 that closes the opening at the lower end of the ventilation pipe 1.

本発明装置において、通気パイプ1の径および
長さは任意であり、必要に応じて適宜定めればよ
い。また通気パイプ1に穿設する気体取入口1b
もその口径は特に限定されず、送通に充分な面積
を確保すればよく、穿設口数も1個に限らない。
この気体取入口は通気パイプ1の上方に設ける
が、パイプ1の端部1eが回転機構との連結に使
用されるため、および液体が気体取入口から入り
込むのを防止する関係で上方側部1bに設けるが
好ましい。
In the device of the present invention, the diameter and length of the ventilation pipe 1 are arbitrary and may be determined as appropriate as necessary. Also, a gas intake port 1b bored in the ventilation pipe 1
The diameter of the hole is not particularly limited, as long as it has a sufficient area for passage, and the number of holes to be drilled is not limited to one.
This gas inlet is provided above the ventilation pipe 1, but since the end 1e of the pipe 1 is used for connection with the rotating mechanism, and in order to prevent liquid from entering through the gas inlet, the upper side 1b is It is preferable to provide the

通気パイプ1の下方側部1cに穿設する気体噴
出口1dは前記気体取入口1bよりも、小口径に
作られており、可及的多数であるのが望ましい。
The gas jet ports 1d formed in the lower side portion 1c of the ventilation pipe 1 are made to have a smaller diameter than the gas intake ports 1b, and preferably as many as possible.

前記インペラー2は前記気体噴出口1dの穿設
距離と同等以上の長さにして通気パイプ1の下方
側部1cに適当手段により固定されるもので、そ
の数は1枚以上で任意に定めてよいが、最も安定
した結果を得るのは4〜8枚を放射状に取付けた
場合である。なお、インペラー2を複数で用いる
場合にはそれらの上端部に補強板2aを配してお
くとよい。またインペラー2の幅も任意に定めて
よく特に限定しない。
The impeller 2 has a length equal to or longer than the drilling distance of the gas outlet 1d, and is fixed to the lower side 1c of the ventilation pipe 1 by appropriate means, and the number of impellers is one or more and can be arbitrarily determined. However, the most stable results are obtained when 4 to 8 sheets are attached radially. In addition, when a plurality of impellers 2 are used, it is preferable to arrange a reinforcing plate 2a at the upper end portions of the impellers 2. Further, the width of the impeller 2 may be arbitrarily determined and is not particularly limited.

通気パイプ1の下端開口部は必ず閉塞されてい
なければならない。これを閉塞する盲板3は単に
前記下端開口部の口径に合せた大きさのものを嵌
合、接着、その他の固定手段により固定するので
足りるが、好ましくは前記インペラー2の幅に合
せた大きさの面積を有するように作り、インペラ
ー2の下端を固定せしめて、インペラー2の補強
を兼ねるようにする(第2図及び4図参照)。
The opening at the lower end of the ventilation pipe 1 must be closed. The blind plate 3 that closes this can be simply fixed by fitting, gluing, or other fixing means with a size that matches the diameter of the lower end opening, but it is preferable that the blind plate 3 has a size that matches the width of the impeller 2. The lower end of the impeller 2 is fixed to serve as reinforcement for the impeller 2 (see FIGS. 2 and 4).

なお本発明装置に用いる材料としては金属、プ
ラスチツクス、セラミツク等が挙げられる。
Note that materials used in the device of the present invention include metals, plastics, ceramics, and the like.

本発明装置は通気パイプ1の頂部を回転機構
(図中省略)に連結せしめて用いる。回転機構の
作動により通気パイプ1を回転せしめ、これによ
りインペラー2が液体中で回転して渦流を生ぜし
め、インペラーの回転方向の背面の液体中に負圧
が生じて気体取入口1bから流入した気体が気体
噴出口1dより噴出し渦流中に混入する。混入し
た気体は渦流とインペラー2の剪断力とにより液
体中に極微粒の気砲を発生させる。
The device of the present invention is used by connecting the top of the ventilation pipe 1 to a rotating mechanism (not shown). The rotation mechanism rotated the ventilation pipe 1, which caused the impeller 2 to rotate in the liquid, creating a vortex, creating negative pressure in the liquid on the back side in the direction of rotation of the impeller, and causing gas to flow in from the gas intake port 1b. Gas is ejected from the gas ejection port 1d and mixed into the vortex. The mixed gas generates extremely fine air particles in the liquid due to the vortex and the shearing force of the impeller 2.

本発明装置は、浄化槽、汚水処理槽、魚類養殖
槽、植物裁培槽等で液体を気体(空気、酸素等)
で処理するのに用いることができる。
The device of the present invention converts liquid into gas (air, oxygen, etc.) in septic tanks, sewage treatment tanks, fish culture tanks, plant culture tanks, etc.
It can be used for processing.

本発明装置は次のような技術的効果を有してい
る。
The device of the present invention has the following technical effects.

(1) 気体を液中に導入するのは自吸式であり、多
量の気体を極微粒気泡として多量液中に発生さ
せることができる。
(1) Gas is introduced into the liquid by a self-priming method, and a large amount of gas can be generated in the form of microscopic bubbles in a large amount of liquid.

(2) インペラーの回転方向の背面に発生する負圧
を応用する構造のため、液中に強力な真空圧を
発生させ、小さなエネルギーで気体を液中に吸
引させることができる。而して水深が2m以上
の所でも容易に目的を達することができる。
(2) The structure utilizes the negative pressure generated on the back side of the impeller in the direction of rotation, so it is possible to generate strong vacuum pressure in the liquid and draw gas into the liquid with a small amount of energy. Therefore, you can easily reach your goal even in places where the water depth is 2 meters or more.

(3) 一度に多量の気体を噴出させることができる
ので強力な上昇流を発生し、周囲の液体に対流
現象を起させ、水槽全体に均一に空気を供給で
きる。
(3) Since a large amount of gas can be ejected at once, a strong upward flow is generated, causing a convection phenomenon in the surrounding liquid, and air can be uniformly supplied throughout the aquarium.

(4) 気体は極微粒化して液体中に混入するため例
えば酸素の溶解効率を高める事ができる。
(4) Since the gas is made into extremely fine particles and mixed into the liquid, the dissolution efficiency of oxygen, for example, can be increased.

(5) 従来曝気装置におけるような液体に流動エネ
ルギーを発生させる構造ではないため、使用エ
ネルギーを大幅に節約できる。
(5) Unlike conventional aeration equipment, the structure does not generate flow energy in the liquid, so energy consumption can be significantly reduced.

(6) 装置内に液体を流入し、噴射させる構造でな
いため、屑物による目詰りがなく、駆動モータ
ーの過負荷を防止しモーター寿命を長くするこ
とができる。また装置に屑物がからまつてもす
ぐ除去できるので長期間の再生利用が可能であ
る。
(6) Since the device does not have a structure in which liquid flows into the device and is injected, there is no clogging with debris, which prevents overload of the drive motor and extends the life of the motor. Furthermore, even if waste gets entangled in the device, it can be removed immediately, allowing for long-term reuse.

(7) 極めて簡単な構造であり、容易に分解組立て
ができ、しかも無給油型であるため、取扱いが
非常に簡単である。
(7) It has an extremely simple structure, can be easily disassembled and assembled, and is oil-free, making it extremely easy to handle.

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

第1図は、従来の気液混合装置の要部を示す一
部縦断側面図、第2図は本発明気液混合装置の実
施態様を示す一部切欠斜視図、第3〜5図は同他
の実施態様を示す一部切欠斜視図である。 図中符号:1…通気パイプ;1b…気体取入
口;1d…気体噴出口;2…インペラー;2a…
補強板;3…盲板。
FIG. 1 is a partially cutaway side view showing the main parts of a conventional gas-liquid mixing device, FIG. 2 is a partially cutaway perspective view showing an embodiment of the gas-liquid mixing device of the present invention, and FIGS. 3 to 5 are the same. FIG. 7 is a partially cutaway perspective view showing another embodiment. Symbols in the figure: 1...Vent pipe; 1b...Gas intake port; 1d...Gas outlet; 2...Impeller; 2a...
Reinforcement plate; 3...Blind plate.

Claims (1)

【特許請求の範囲】[Claims] 1 上方に気体取入口を有し且つ下方側部に複数
の気体噴出孔を穿設した通気パイプと、前記通気
パイプに沿う様通気パイプの下方側部に固定した
インペラーと、通気パイプの下端開口部を閉塞す
る盲板とを有して成ることを特徴とする気液混合
装置。
1. A ventilation pipe having a gas intake port on the upper side and a plurality of gas ejection holes on the lower side, an impeller fixed to the lower side of the ventilation pipe along the ventilation pipe, and an opening at the lower end of the ventilation pipe. 1. A gas-liquid mixing device comprising: a blind plate that closes a portion of the gas-liquid mixing device.
JP58032890A 1983-03-02 1983-03-02 Gas-liquid mixing device Granted JPS59160516A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58032890A JPS59160516A (en) 1983-03-02 1983-03-02 Gas-liquid mixing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58032890A JPS59160516A (en) 1983-03-02 1983-03-02 Gas-liquid mixing device

Publications (2)

Publication Number Publication Date
JPS59160516A JPS59160516A (en) 1984-09-11
JPS6234436B2 true JPS6234436B2 (en) 1987-07-27

Family

ID=12371473

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58032890A Granted JPS59160516A (en) 1983-03-02 1983-03-02 Gas-liquid mixing device

Country Status (1)

Country Link
JP (1) JPS59160516A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007029803A (en) * 2005-07-25 2007-02-08 Asahi Organic Chem Ind Co Ltd Apparatus for dispersing insoluble matter

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4990166A (en) * 1989-06-08 1991-02-05 Babich William F Gas stream purifying equipment
JP5632991B2 (en) * 2009-06-24 2014-12-03 有限会社こうすい Microbubble generator
JP5704430B2 (en) * 2010-08-07 2015-04-22 和順 佐藤 Gas-liquid and liquid-liquid mixing apparatus and method
KR101867678B1 (en) * 2016-07-27 2018-06-15 주식회사 포스코 Mixing apparatus
JP7105445B2 (en) * 2018-10-04 2022-07-25 住友金属鉱山株式会社 Reactor

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5424133U (en) * 1977-07-20 1979-02-16
JPS54110163U (en) * 1978-01-23 1979-08-02

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007029803A (en) * 2005-07-25 2007-02-08 Asahi Organic Chem Ind Co Ltd Apparatus for dispersing insoluble matter

Also Published As

Publication number Publication date
JPS59160516A (en) 1984-09-11

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