JP3081983B2 - Fine bubble generator - Google Patents

Fine bubble generator

Info

Publication number
JP3081983B2
JP3081983B2 JP06319425A JP31942594A JP3081983B2 JP 3081983 B2 JP3081983 B2 JP 3081983B2 JP 06319425 A JP06319425 A JP 06319425A JP 31942594 A JP31942594 A JP 31942594A JP 3081983 B2 JP3081983 B2 JP 3081983B2
Authority
JP
Japan
Prior art keywords
pump
pressure
water
air
discharge pressure
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
JP06319425A
Other languages
Japanese (ja)
Other versions
JPH08155436A (en
Inventor
井 一 郎 高
村 浩 之 高
Original Assignee
日本技建株式会社
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Filing date
Publication date
Application filed by 日本技建株式会社 filed Critical 日本技建株式会社
Priority to JP06319425A priority Critical patent/JP3081983B2/en
Publication of JPH08155436A publication Critical patent/JPH08155436A/en
Application granted granted Critical
Publication of JP3081983B2 publication Critical patent/JP3081983B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Physical Water Treatments (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】本発明は排水処理分野における浮
上分離装置としての微細気泡発生装置、および各種産業
分野における微細気泡発生装置、気体溶解装置等の各種
分野に利用される微細気泡発生装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a microbubble generator as a flotation separator in the field of wastewater treatment and a microbubble generator used in various fields such as a microbubble generator and a gas dissolving apparatus in various industrial fields. .

【0002】[0002]

【従来の技術】従来の気泡発生装置は、水中に潜在的に
溶解している気体を減圧することによって気泡として発
生させる装置、あるいは特殊な耐圧容器内において水に
加圧気体を強制的に溶解させた後に常圧状態に戻すこと
で気泡を発生させる装置等が用いられている(以下前者
という)。
2. Description of the Related Art A conventional bubble generating device is a device for generating gas by depressurizing a gas that is potentially dissolved in water, or forcibly dissolving a pressurized gas in water in a special pressure vessel. An apparatus or the like that generates air bubbles by returning the pressure to a normal pressure state after use (hereinafter, referred to as the former) is used.

【0003】また別の気泡微細化分散装置として、槽内
に気液混合を目的としたノズルを吐出部に有する送水ポ
ンプを配置したような装置(実開平4−57300号公
報等)がある(以下後者という)。
[0003] As another bubble atomizing and dispersing apparatus, there is an apparatus in which a water pump having a nozzle for gas-liquid mixing at a discharge portion is disposed in a tank (Japanese Utility Model Laid-Open No. 4-57300). Hereinafter the latter).

【0004】[0004]

【発明が解決しようとする課題】前者の気泡発生装置
は、減圧・加圧状態を発生させる為の強力なブロア−・
コンプレッサ−等の圧力制御装置が必要とされる上、プ
ロセス上に減圧タンクあるいは加圧タンクが必要である
ために、装置運転時のエネルギ−消費量が大きい。
装置規模が大がかりとなり、小型化が困難。エネルギ
−消費に伴う動力コストが高い。ブロア−・コンプレ
ッサ−運転に伴い騒音が発生するというような欠点があ
った。
The former air bubble generator is a powerful blower for generating a depressurized / pressurized state.
In addition to the need for a pressure control device such as a compressor and the need for a decompression tank or a pressurized tank in the process, energy consumption during operation of the device is large.
The scale of the device becomes large, and miniaturization is difficult. Power costs associated with energy consumption are high. There is a drawback that noise is generated with the operation of the blower compressor.

【0005】また、後者の気泡微細化分散装置は、気
泡と水の単純な混合操作では、気泡の微細化が十分では
なく、気泡径が1mm以下の微細な気泡は実質的には得
ることが難しい。排水処理分野における固液分離装置
に使用した場合には、槽内水を気泡発生用水として循環
利用するような構造としたとき、送水ポンプ内部での回
転翼による強撹拌による固形分の破壊や、送水ポンプよ
り吐出される激しい水流の発生によって固形物が分散
し、処理された水の水質が悪化するというような欠点が
あった。
[0005] In addition, the latter air bubble dispersing and dispersing apparatus is not capable of sufficiently reducing air bubbles by a simple mixing operation of air bubbles and water, and is capable of substantially obtaining fine air bubbles having a diameter of 1 mm or less. difficult. When used in a solid-liquid separator in the wastewater treatment field, when the water in the tank is circulated and used as bubble generation water, the solid content is destroyed by strong stirring by the rotating blades inside the water supply pump, There is a drawback that the solid matter is dispersed due to the generation of a violent water flow discharged from the water supply pump, and the quality of the treated water deteriorates.

【0006】本発明は上記の問題点に鑑みてなされたも
ので、簡易な構造にして小型で、排水処理分野における
浮上分離装置や各種産業分野における微細気泡発生装
置、気体溶解装置等の各種分野に適用するのに理想的な
微細気泡が得られる微細気泡発生装置を提供することを
目的とする。
SUMMARY OF THE INVENTION The present invention has been made in view of the above problems, and has a simple structure and a small size, and is used in various fields such as a flotation apparatus in a wastewater treatment field, a microbubble generator in various industrial fields, and a gas dissolution apparatus. It is an object of the present invention to provide a microbubble generating device which can obtain microbubbles ideal for application to a device.

【0007】[0007]

【課題を解決するための手段】本発明に係る微細気泡発
生装置は、一方が高吐出圧力で、他方が低吐出圧力であ
る吐出圧力の異なる2台の回転翼を有するポンプのそれ
ぞれの吐出口を耐圧配管にて接続し、前記ポンプのうち
高吐出圧力のポンプの吸引口にエアとともに水を供給す
る供給管を接続し、低吐出圧力のポンプの吸引口に、流
量及び圧力制御を行う流量調整バルブを備えたノズルを
設置し、両ポンプの稼動時の圧力差を利用して前記ノズ
ルから微細気泡を発生させるようにしたものである。
According to the present invention, there is provided a microbubble generator according to the present invention, wherein each discharge port of a pump having two rotating blades having different discharge pressures, one of which has a high discharge pressure and the other has a low discharge pressure. Is connected by a pressure-resistant pipe, a supply pipe for supplying water together with air is connected to a suction port of a pump having a high discharge pressure among the pumps, and a flow rate for controlling flow rate and pressure is connected to a suction port of a pump having a low discharge pressure. A nozzle provided with an adjustment valve is provided, and fine bubbles are generated from the nozzle by utilizing a pressure difference when both pumps are operated.

【0008】また前記高吐出圧力のポンプの吸引口に接
続した供給管には、エアの定量的な混合を行う小型のエ
ア−ポンプと流量調節機能を有した送気ノズルを接続す
る。さらに前記2台の回転翼を有するポンプは渦巻きポ
ンプであって、低吐出圧力のポンプを水槽内に設置又は
水上に浮上設置する。
A small air pump for quantitatively mixing air and an air supply nozzle having a flow rate adjusting function are connected to a supply pipe connected to the suction port of the high discharge pressure pump. Further, the pump having the two rotating blades is a centrifugal pump, and a pump having a low discharge pressure is installed in a water tank or floated above water.

【0009】[0009]

【作用】本発明に係る微細気泡発生装置は、基本原理に
ついては前記従来技術の項の前者で説明した加圧気泡発
生装置のように加圧下で気体を水中に溶解させた後に常
圧下まで圧力を下げ、各圧力下の気体の飽和溶解度の差
分の気体を気泡として析出させるという点は共通してい
る。しかし、上記した前者の従来の加圧気泡発生装置は
強力なコンプレッサ−を使用するのに対して、本発明に
係る微細気泡発生装置は一方が高吐出圧力で、他方が低
吐出圧力である吐出圧力の異なる2台の回転翼を有する
ポンプのそれぞれの吐出口を耐圧配管にて接続し、双方
のポンプを同時に運転することにより接続した耐圧配管
内部において圧力差が生じるようにしている。
The microbubble generator according to the present invention has a basic principle in which a gas is dissolved in water under pressure as in the pressurized bubble generator described in the former of the prior art section, and then the pressure is reduced to normal pressure. It is common that the gas having the difference in the saturation solubility of the gas under each pressure is precipitated as bubbles. However, while the former conventional pressurized bubble generator uses a powerful compressor, the microbubble generator according to the present invention has a discharge at one high discharge pressure and another at a low discharge pressure. The discharge ports of the pumps having two rotating blades having different pressures are connected by pressure-resistant pipes, and by operating both pumps simultaneously, a pressure difference is generated inside the connected pressure-resistant pipes.

【0010】高吐出圧力の回転翼を有するポンプの吸引
口を本装置の吸引口として、低吐出圧力の回転翼を有す
るポンプの吸引口を本装置の吐出口として機能させ本装
置の吸引口にはエアの定量的な混合を目的とした小型の
エア−ポンプと流量調節機能を有した送気ノズルを取付
け、本装置の吐出口には流量及び本装置内部の圧力制御
を目的とした流量調節バルブを備えたノズルを装備して
おり、強力なコンプレッサ−や加圧タンク等を使用しな
いでも気体を水中に溶解させることを可能にすること
で、前述した問題点の改善を実現している。
The suction port of a pump having rotating blades of high discharge pressure functions as a suction port of the apparatus, and the suction port of a pump having rotating blades of low discharge pressure functions as a discharge port of the apparatus. Is equipped with a small air pump for quantitative mixing of air and an air supply nozzle with a flow rate control function, and a flow rate control at the discharge port of this device for the purpose of controlling the flow rate and the pressure inside the device. A nozzle equipped with a valve is provided, which enables the gas to be dissolved in water without using a powerful compressor, a pressurized tank, or the like, thereby realizing the above-mentioned problem.

【0011】[0011]

【実施例】以下に本発明の一実施例を図面に基づいて具
体的に説明する。 (装置の構成)水槽8(本例では幅400mm×長さ7
00mm×深さ500mm、有効容積120リットルの
ものを使用したが必ずしもこのサイズに限定されるもの
ではない)の壁面にとりつけられたフランジ13を介し
て側壁に貫通する配管の水槽8の外側部分の末端には吐
出水量が例えば5m3 /hr、吐出水圧5kgf/cm
2 の能力を持つ多段式渦巻きポンプ1(高吐出圧力の回
転翼を有するポンプをいう)(ポンプは回転翼を有する
ものであれば渦巻き式に限定されない)の吐出口を、槽
内部側の末端には吐出水量が例えば10m3 /hr、吐
出水圧1kgf/cm2 の能力を持つ水中渦巻きポンプ
4(低吐出圧力の回転翼を有するポンプをいう)(ポン
プは回転翼を有するものであれば渦巻き式に限定されな
い)の吐出口を接続する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be specifically described below with reference to the drawings. (Structure of the device) A water tank 8 (400 mm wide × 7 long in this example)
(00 mm × 500 mm in depth and an effective volume of 120 liters were used, but the size is not necessarily limited to this). At the end, the discharge water amount is, for example, 5 m 3 / hr, and the discharge water pressure is 5 kgf / cm.
The discharge port of the multi-stage centrifugal pump 1 having a capacity of 2 (refers to a pump having rotary blades with high discharge pressure) (the pump is not limited to the spiral type as long as it has rotary blades) Is a submersible centrifugal pump 4 having a capacity of, for example, 10 m 3 / hr and a discharge water pressure of 1 kgf / cm 2 (refers to a pump having a rotary blade with a low discharge pressure). (Not limited to the formula).

【0012】高吐出圧力の回転翼を有するポンプ1の吸
引口は水を満たした別の水槽14へ水供給配管9で結
ぶ。高吐出圧力の回転翼を有するポンプ1の吸引口には
乾電池式の小型エアポンプ10よりエア供給配管11を
結び、定量的に気体を圧送できるようにしておく。ただ
しこの時のエア−ポンプの能力は水供給配管9とエア供
給配管11の接続部とこれに接続される水槽14の水面
の差による水圧に打ち勝つ程度で足り、家庭用の養魚水
槽で使用されている即ち1000ml/分以下の吐出能
力でも可能である。低吐出圧力の回転翼を有するポンプ
4の吸引口6、即ち本装置の吐出口には流量の調節及び
運転時の圧力調整を目的とした流量調節バルブ12を備
えたノズル(図示せず)を設置した。
The suction port of the pump 1 having the rotary blades with high discharge pressure is connected by a water supply pipe 9 to another water tank 14 filled with water. An air supply pipe 11 is connected to a suction port of the pump 1 having a rotating blade with a high discharge pressure from a small-sized air pump 10 of a dry cell type so that gas can be pumped quantitatively. However, the capacity of the air pump at this time is sufficient to overcome the water pressure due to the difference in water level between the connection between the water supply pipe 9 and the air supply pipe 11 and the water tank 14 connected thereto, and is used in a domestic fish tank. That is, a discharge capacity of 1000 ml / min or less is also possible. A nozzle (not shown) provided with a flow rate control valve 12 for the purpose of flow rate adjustment and pressure adjustment during operation is provided at the suction port 6 of the pump 4 having a rotor blade with a low discharge pressure, that is, the discharge port of the present apparatus. installed.

【0013】(装置の運転)ここで双方のポンプ1、4
を同時に始動すると、各ポンプとも水の吸引を開始する
がポンプ4はポンプ1の吐出圧より低いからポンプ1よ
り送られる水はポンプ4の内部をポンプ本来の流れ方向
とは逆に流れ、ポンプ4の吸引口、即ち本装置の吐出口
6より例えば1m3 /hrで吐出される。この際それぞ
れのポンプ1、4を接続する耐圧配管7の内部にはポン
プ4の吐出圧能力と等しい例えば1kgf/cm2 の圧
力が発生するはずであるが、ポンプ4の吸引口、即ち本
装置の吐出口に設けた流量調節バルブ12を備えたノズ
ル(図示せず)を水が通過する際に通過抵抗を生じ、管
内の圧力は例えば4kgf/cm2 にまで達する。
(Operation of the apparatus) Here, both pumps 1, 4
At the same time, each pump starts suctioning water. However, since the pump 4 is lower than the discharge pressure of the pump 1, the water sent from the pump 1 flows inside the pump 4 in a direction opposite to the original flow direction of the pump. The liquid is discharged from the suction port 4, that is, the discharge port 6 of the present apparatus at, for example, 1 m 3 / hr. At this time, a pressure of, for example, 1 kgf / cm 2 , which is equal to the discharge pressure capability of the pump 4, should be generated inside the pressure-resistant pipe 7 connecting the respective pumps 1, 4. When water passes through a nozzle (not shown) provided with a flow rate control valve 12 provided at the discharge port, a passage resistance is generated, and the pressure in the pipe reaches, for example, 4 kgf / cm 2 .

【0014】(気泡の発生)ポンプ1の吸引口に接続さ
れている水供給配管9にはエア供給配管11を通して乾
電池式の小型エアポンプ10で例えば200〜500c
c/分程度の気体を定量的に圧送する。気体は水と混合
され直径数mmの気泡となってポンプ1内部に供給され
る。気泡はポンプ1内部の回転翼によって破壊され、例
えば直径1〜2mm程度になる。接続された耐圧配管7
の内部は例えば4kgf/cm2 の加圧状態となってい
るために、気体は飽和溶解濃度まで水中に溶解する。圧
力が例えば4kgf/cm2 下で気体が溶解した水はポ
ンプ4の内部を通り、該ポンプ4の回転翼によって再度
分散し、最後に流量調節バルブ12を備えたノズル(図
示せず)を通過して水槽内に吐出されると、加圧状態か
ら常圧環境に放出される。こうして分散化した気体を溶
解した水が該ノズルから吐出されると周囲圧力が常圧状
態まで下がるから、常圧の気体の飽和溶解量以上に溶解
していた気体は、直径が例えば0.1mm(100μ
m)以下の微細な気泡として析出する。
(Generation of Air Bubbles) A dry battery type small air pump 10 passes through a water supply pipe 9 connected to a suction port of the pump 1 through an air supply pipe 11, for example, 200 to 500 c.
A gas of about c / min is quantitatively pumped. The gas is mixed with water to form bubbles having a diameter of several mm and supplied to the inside of the pump 1. Bubbles are destroyed by the rotating blades inside the pump 1 and become, for example, about 1 to 2 mm in diameter. Connected pressure-resistant pipe 7
Is pressurized at, for example, 4 kgf / cm 2 , so that the gas dissolves in water to a saturated dissolution concentration. The water in which the gas is dissolved at a pressure of, for example, 4 kgf / cm 2 passes through the inside of the pump 4, is dispersed again by the rotating blades of the pump 4, and finally passes through a nozzle (not shown) equipped with a flow control valve 12. Then, when discharged into the water tank, it is released from the pressurized state to the normal pressure environment. When the water in which the gas thus dispersed is dissolved is discharged from the nozzle, the ambient pressure is reduced to a normal pressure state. (100μ
m) Precipitates as the following fine bubbles.

【0015】本装置を例えば40秒間運転すると、水槽
8内部の水は微細な気泡によって水中を通過する光が散
乱されて白濁する。発生する気泡が細かく、かつ多量で
あるほど光の散乱度合いが大きくなるため光の到達距離
は短くなる。本装置が例えば40秒間に吐出する水量は
約11リットルであり、混合される水量は水槽8の有効
容積が例えば120リットルの10%に相当する。本装
置と、従来のコンプレッサ−と加圧タンクを使用した
気泡発生装置と、従来の気液混合ノズルと送水ポンプ
を使用した加圧浮上式気泡発生装置とのそれぞれを同
条件で運転してレ−ザ−光(波長780nm)の光到達
距離を比較した結果を表1に示す。
When this apparatus is operated for 40 seconds, for example, the water in the water tank 8 becomes turbid because light passing through the water is scattered by fine bubbles. The smaller and larger the amount of generated bubbles, the greater the degree of light scattering, and thus the shorter the reach of light. For example, the amount of water discharged by the present apparatus for 40 seconds is about 11 liters, and the amount of water to be mixed corresponds to an effective volume of the water tank 8 of, for example, 10% of 120 liters. The present apparatus, a conventional bubble generator using a compressor and a pressurized tank, and a conventional air-bubble bubble generator using a gas-liquid mixing nozzle and a water pump are operated under the same conditions, and operated. Table 1 shows the results of comparing the light reaching distances of the light (wavelength 780 nm).

【0016】[0016]

【表1】 [Table 1]

【0017】表1で示されるように、本装置において発
生する気泡の形態・量は加圧浮上法に用いられる気泡発
生装置と同等であることが確認されている。
As shown in Table 1, it has been confirmed that the form and amount of bubbles generated in the present apparatus are equivalent to those of the bubble generating apparatus used in the pressure flotation method.

【0018】また水槽8内部にパルプを分散させた状態
で本装置と前述した従来の2種類の気泡発生装置、
で気泡を発生させて気泡がパルプ繊維に付着して水面
上に浮上させる能力を比較した。水槽8に100mg/
lのパルプ粉を投入し、各装置から40秒間気泡を導入
した後、5分間静置して浮上したパルプ繊維成分を除去
した後に水中に残留しているパルプ濃度を比較した結果
を表2に示す。
In a state where the pulp is dispersed in the water tank 8, the present apparatus and the above-described conventional two types of bubble generating apparatuses are provided.
The ability to generate air bubbles and cause the air bubbles to adhere to the pulp fiber and float on the water surface was compared. 100 mg /
l of pulp powder was introduced, air bubbles were introduced from each device for 40 seconds, and then the pulp fiber component remaining in water after removing the pulp fiber component which floated by standing still for 5 minutes is shown in Table 2. Show.

【0019】[0019]

【表2】 [Table 2]

【0020】上記表2で示されるように、本装置は微細
気泡による分離効果についても加圧浮上法に用いられる
気泡発生装置と同等の能力を有していることが確認され
た。
As shown in the above Table 2, it was confirmed that the present apparatus also had the same effect as the bubble generating apparatus used in the pressure flotation method in terms of the separation effect by the fine bubbles.

【0021】[0021]

【発明の効果】本発明に係る微細気泡発生装置は、一方
が高吐出圧力で、他方が低吐出圧力である吐出圧力の異
なる2台の回転翼を有するポンプのそれぞれの吐出口を
耐圧配管にて接続し、前記ポンプのうち高吐出圧力のポ
ンプの吸引口にエアとともに水を供給する供給管を接続
し、低吐出圧力のポンプの吸引口に、流量及び圧力制御
を行う流量調整バルブを備えたノズルを設置し、両ポン
プの稼動時の圧力差を利用して前記ノズルから微細気泡
を発生させるようにしたので、市販のポンプを利用した
簡単な構造で、水中に気体を溶解させることができ、低
吐出圧力の回転翼を有するポンプより常圧の水槽内に、
その圧力差による過飽和状態となった気体を直径0.1
mm未満の非常に小さな微細気泡として発生させること
ができ、様々な分野に対して優れた効果を発揮する。
According to the microbubble generator according to the present invention, each discharge port of a pump having two rotating blades having different discharge pressures, one of which has a high discharge pressure and the other has a low discharge pressure, is connected to a pressure-resistant pipe. A supply pipe for supplying water together with air to a suction port of a pump having a high discharge pressure among the pumps, and a flow control valve for performing flow rate and pressure control is provided at a suction port of the pump having a low discharge pressure. A nozzle was installed, and fine bubbles were generated from the nozzle using the pressure difference during the operation of both pumps, so that gas can be dissolved in water with a simple structure using a commercially available pump. In a water tank at normal pressure than a pump having a rotor with low discharge pressure,
The gas that has become supersaturated due to the pressure difference has a diameter of 0.1
It can be generated as very small microbubbles of less than mm, and exhibits excellent effects in various fields.

【0022】また本発明に係る微細気泡発生装置の構造
そのものは2台の回転翼を有するポンプを向かい合わせ
た状態を基本とした簡易なものであるために、小型化が
容易であり、強力なコンプレッサ−を必要としないで済
み、運転コストも低く押えることが可能である。特に、
排水処理における浮上分離法に適用すれば、発生する気
泡の状態は従来の加圧浮上法に匹敵する気泡を発生させ
ることが出来る上、装置構造が単純かつ小型であるため
に中小規模の装置へも導入が実現可能である。
Further, the structure of the microbubble generator according to the present invention is a simple structure based on a pump having two rotating blades facing each other. The need for a compressor is eliminated, and the operating cost can be kept low. In particular,
If applied to the flotation separation method in wastewater treatment, the state of generated bubbles can generate bubbles comparable to the conventional pressure flotation method.In addition, because the device structure is simple and small, it can be applied to small and medium-sized devices. The introduction is also feasible.

【0023】また養魚分野等における気体溶解装置とし
て使用すると、吐出される水は、気体が飽和濃度状態で
あるから、溶解気体を豊富に含む水の供給装置として利
用することが出来る。さらに小型でかつ安価であるため
に、設置スペ−スが限定されるような小規模の付帯装置
として幅広く利用することが出来る。
Further, when used as a gas dissolving apparatus in the field of fish farming, the discharged water can be used as a water supplying apparatus rich in dissolved gas since the gas is in a saturated concentration state. Further, since it is small and inexpensive, it can be widely used as a small-scale auxiliary device having a limited installation space.

【0024】さらに前記高吐出圧力のポンプの吸引口に
接続した供給管に、小型のエア−ポンプと送気ノズルを
接続することによりエアの定量的な混合が確実に行わ
れ、かつ流量調節も適切に行うことができ、連続的な稼
動が可能となる。
Furthermore, by connecting a small air pump and an air supply nozzle to a supply pipe connected to the suction port of the high discharge pressure pump, quantitative mixing of air is reliably performed, and flow rate is adjusted. It can be performed properly and can be operated continuously.

【0025】そして前記2台の回転翼を有するポンプは
渦巻きポンプであって、低吐出圧力のポンプを水槽内に
設置又は水上に浮上設置することにより、市販のポンプ
の利用が可能となり、低吐出圧力のポンプの設置スペ−
スを水槽の外に確保する必要がなく、よりコンパクト化
が図れる。
The pump having the two rotors is a centrifugal pump. By installing a pump having a low discharge pressure in a water tank or floating above the water, a commercially available pump can be used. Pressure pump installation space
There is no need to secure the outside of the water tank, and a more compact design can be achieved.

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

【図1】本発明の一実施例を示す概略説明図である。FIG. 1 is a schematic explanatory view showing one embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 高吐出圧力の渦巻きポンプ 2 高吐出圧力の渦巻きポンプ吸引口(本装置の吸引
口) 3 高吐出圧力の渦巻きポンプ吐出口 4 低吐出圧力の渦巻きポンプ 5 渦巻きポンプ吐出口 6 渦巻きポンプ吸引口(本装置の吐出口) 7 耐圧配管 8 水槽 9 水供給配管 10 小型エア−ポンプ 11 エア供給配管 12 流量調節バルブ 13 フランジ 14 別の水槽
1 high discharge pressure spiral pump 2 high discharge pressure spiral pump suction port (suction port of this device) 3 high discharge pressure spiral pump discharge port 4 low discharge pressure spiral pump 5 spiral pump discharge port 6 spiral pump suction port (Discharge port of this device) 7 Pressure-resistant pipe 8 Water tank 9 Water supply pipe 10 Small air pump 11 Air supply pipe 12 Flow control valve 13 Flange 14 Another water tank

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 一方が高吐出圧力で、他方が低吐出圧力
である吐出圧力の異なる2台の回転翼を有するポンプの
それぞれの吐出口を耐圧配管にて接続し、前記ポンプの
うち高吐出圧力のポンプの吸引口にエアとともに水を供
給する供給管を接続し、低吐出圧力のポンプの吸引口
に、流量及び圧力制御を行う流量調整バルブを備えたノ
ズルを設置し、両ポンプの稼動時の圧力差を利用して前
記ノズルから微細気泡を発生させることを特徴とする微
細気泡発生装置。
1. A pump having two discharge blades having different discharge pressures, one of which has a high discharge pressure and the other of which has a low discharge pressure, has respective discharge ports connected by pressure-resistant piping. A supply pipe that supplies water together with air is connected to the suction port of the pressure pump, and a nozzle equipped with a flow rate adjustment valve that controls the flow rate and pressure is installed at the suction port of the low discharge pressure pump. A microbubble generator, wherein microbubbles are generated from the nozzle using a pressure difference at the time.
【請求項2】 前記高吐出圧力のポンプの吸引口に接続
した供給管に、エアの定量的な混合を行う小型のエア−
ポンプと流量調節機能を有した送気ノズルを接続したこ
とを特徴とする請求項1記載の微細気泡発生装置。
2. A small air pump for quantitatively mixing air into a supply pipe connected to a suction port of the high discharge pressure pump.
2. The microbubble generator according to claim 1, wherein a pump and an air supply nozzle having a flow control function are connected.
【請求項3】 前記2台の回転翼を有するポンプは渦巻
きポンプであって、低吐出圧力のポンプを水槽内に設置
又は水上に浮上設置することを特徴とする請求項1記載
の微細気泡発生装置。
3. The microbubble generation according to claim 1, wherein the pump having two rotating blades is a centrifugal pump, and a pump having a low discharge pressure is installed in a water tank or installed floating on water. apparatus.
JP06319425A 1994-11-30 1994-11-30 Fine bubble generator Expired - Fee Related JP3081983B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP06319425A JP3081983B2 (en) 1994-11-30 1994-11-30 Fine bubble generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06319425A JP3081983B2 (en) 1994-11-30 1994-11-30 Fine bubble generator

Publications (2)

Publication Number Publication Date
JPH08155436A JPH08155436A (en) 1996-06-18
JP3081983B2 true JP3081983B2 (en) 2000-08-28

Family

ID=18110056

Family Applications (1)

Application Number Title Priority Date Filing Date
JP06319425A Expired - Fee Related JP3081983B2 (en) 1994-11-30 1994-11-30 Fine bubble generator

Country Status (1)

Country Link
JP (1) JP3081983B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101804309A (en) * 2010-03-26 2010-08-18 上海师范大学 Method and device for preparing nano-bubbles by water temperature difference method

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4815032B2 (en) * 2006-01-17 2011-11-16 敏夫 宮下 Microbubble generator and gas-liquid mixing tank

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101804309A (en) * 2010-03-26 2010-08-18 上海师范大学 Method and device for preparing nano-bubbles by water temperature difference method
CN101804309B (en) * 2010-03-26 2012-08-29 上海师范大学 Method and device for preparing nano-bubbles by water temperature difference method

Also Published As

Publication number Publication date
JPH08155436A (en) 1996-06-18

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