JPS638475Y2 - - Google Patents

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Publication number
JPS638475Y2
JPS638475Y2 JP7575682U JP7575682U JPS638475Y2 JP S638475 Y2 JPS638475 Y2 JP S638475Y2 JP 7575682 U JP7575682 U JP 7575682U JP 7575682 U JP7575682 U JP 7575682U JP S638475 Y2 JPS638475 Y2 JP S638475Y2
Authority
JP
Japan
Prior art keywords
water
air
pipe
jet
nozzle
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
JP7575682U
Other languages
Japanese (ja)
Other versions
JPS58178396U (en
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 filed Critical
Priority to JP1982075756U priority Critical patent/JPS58178396U/en
Publication of JPS58178396U publication Critical patent/JPS58178396U/en
Application granted granted Critical
Publication of JPS638475Y2 publication Critical patent/JPS638475Y2/ja
Granted legal-status Critical Current

Links

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

Description

【考案の詳細な説明】 此の考案は溶存酸素の増加により汚水を浄化す
る空中撒布型のジエツト吸気旋回流曝気装置に関
する。近年湖沼、貯水池、養魚池等に産業廃水、
下水道放流水、家庭雑用水等の流入が激しく、自
浄作用の限界を超え、水質汚濁化が進み、環境衛
生上は勿論水資源の水質保全上又は魚類生産上か
らみて非常に問題となつている。此の汚濁した水
質を浄化する方法には種々の方法が提案されてい
るが、曝気により溶存酸素の増加をはかる方法は
その最も有効な方法であるといえる。特に養魚場
の鼻上げ時には必須の方法である。
[Detailed Description of the Invention] This invention relates to an air spray type jet intake swirl flow aeration device that purifies wastewater by increasing dissolved oxygen. In recent years, industrial wastewater has been flowing into lakes, reservoirs, fish ponds, etc.
The influx of sewage discharge water, household water, etc. is intense, exceeding the limits of self-purification, resulting in water pollution, which is becoming a serious problem not only from the standpoint of environmental hygiene but also from the standpoint of water quality conservation and fish production. . Various methods have been proposed to purify this polluted water, but the method of increasing dissolved oxygen through aeration can be said to be the most effective method. This is an essential method especially when raising fish farms.

本考案装置は以上の曝気作用を最も効率よく実
施する装置に関するものであつて、水底に設置さ
れた水中ポンプより水面に浮ぶ環状ノツズルにい
たる送水可撓管中に吐出圧力水のジエツト作用に
より大気を吸引し、更に螺旋羽根管により旋回流
をおこして吐出水と吸引大気とを可撓管内で旋回
しつつ気液混合させ、これを環状ノツズルより大
気中に撒布放出することを特徴とするジエツト吸
気旋回流曝気装置を特徴とする。
The device of the present invention is a device that most efficiently performs the aeration described above, and uses the jet action of pressurized water to pump air into the flexible water pipe that extends from the submersible pump installed at the bottom of the water to the annular nozzle floating on the water surface. The jet is characterized by sucking in water, creating a swirling flow using a spiral vane tube, mixing the discharged water and the suctioned atmosphere in a flexible tube while swirling the gas and liquid, and discharging the mixture into the atmosphere from an annular nozzle. Features an intake swirl flow aeration device.

従来此の種の装置としては (1) 空気飛散方式 ポンプ吐出圧力水をノツズル、多孔パイプ等か
ら空中に飛散撒布させ空気中の酸素と原水を接触
させる方式。
Conventional devices of this type include: (1) Air splash method A method in which pump discharge pressure water is splashed into the air from a nozzle, perforated pipe, etc. to bring oxygen in the air into contact with raw water.

(2) 強制給気方式 水中に圧力空気源と接続した撒気板、撒気箇、
多孔板、ノツズル、ジエツト、細孔付きパイプ等
を設置し、圧力空気を強制的に水中に吹き込み水
と空気を接触させる方式。
(2) Forced air supply system: An air supply plate, air supply point, etc. connected to a pressure air source underwater.
A method in which perforated plates, nozzles, jets, pipes with small holes, etc. are installed, and pressurized air is forced into the water to bring the water into contact with the air.

(3) 機械的表面曝気方式 羽根車等を水面に設置してこれを回転させるこ
とにより水面を機械的に撹拌する方式。
(3) Mechanical surface aeration method A method that mechanically agitates the water surface by installing an impeller on the water surface and rotating it.

(4) ジエツト方式 ポンプ吐出側にジエツトノツズルを取つけ大気
をエジエクター作用により吸引して吐出水中に混
合接触させる方式。
(4) Jet method A method in which a jet nozzle is attached to the discharge side of the pump, and atmospheric air is sucked in by the ejector action and brought into contact with the discharged water.

(5) ジエツトエアレーター方式 ポンプの吐出側にジエツトノツズルを設けジエ
ツト流中に圧力空気を吹き込み気液混合して放出
する方式。
(5) Jet aerator method A jet nozzle is installed on the discharge side of the pump, and pressurized air is blown into the jet flow to mix gas and liquid and discharge the mixture.

等が提案実施されているが (1) 空中飛散方式はノツズル又は多孔パイプから
噴出するのみで大気との接触時間及び接触率が
少なく酸素溶解効率が低い。
(1) The aerial dispersion method only ejects from a nozzle or porous pipe, so the contact time and contact rate with the atmosphere is short, and the oxygen dissolution efficiency is low.

(2) 強制給気方式は微細気泡を発生するため使用
する撒気板、撒布筒の材質が緻密構造のため、
通過抵抗による圧力損失が大きく、更に圧力空
気源を停止するときは逆流による土砂の目詰り
等が多く、更に発生する微細気泡は上昇するの
みで横方向への移動は少く汚水に対する酸化の
影響範囲が限定されており、又多孔板、ノツズ
ル、ジエツト、細孔付きパイプ等は微細気泡を
発生しないか又は発生しても水との接触時間が
短かく酸素溶解効率は低い。
(2) The forced air supply method generates fine air bubbles, so the materials used for the air blowing plate and blowing tube are dense, so
The pressure loss due to passage resistance is large, and when the pressurized air source is stopped, there is a lot of clogging with earth and sand due to backflow.Furthermore, the microbubbles that are generated only rise and do not move laterally, which limits the range of oxidation effects on wastewater. In addition, perforated plates, nozzles, jets, pipes with fine holes, etc. either do not generate microbubbles, or even if they do, the contact time with water is short and the oxygen dissolution efficiency is low.

(3) 機械的表面曝気方式は表層水が主で深層用水
には不適である。
(3) The mechanical surface aeration method is mainly used for surface water and is not suitable for deep water.

(4) ジエツト方式、(5)ジエツトエアレーター方式
いづれも噴出方向が一方的なものが多くその影
響する範囲が局部的で広水域汚濁水の浄化には
不適である。特にジエツトエアレーター方式は
他の圧力空気源を必要とする。
In both the (4) jet method and (5) jet aerator method, the ejection direction is often one-sided, and the area of influence is localized, making them unsuitable for purifying polluted water in a wide area. In particular, jet aerator systems require other sources of pressurized air.

本考案は簡単な手段により上記各方式の欠点を
除去した広水域に利用できる酸素溶解効率のよい
曝気装置の提供を目的としている。
The object of the present invention is to provide an aeration device with high oxygen dissolution efficiency that can be used in wide areas and eliminates the drawbacks of the above-mentioned systems by simple means.

此の考案の装置を図面にもとづいて説明する
と、水面上に浮んだフロート1にノツズル取付け
バンド2、締結バンド3により締結された下部円
錐4とその円錐部下端内部に設けた三脚支持板5
に調整間座7により間隔を調整してボルト及びナ
ツト8で結合された上部円錐9とより構成される
載頭円錐形環状ノツズルに送水可撓管6を締結バ
ンド10で締結する。同じく水底に設置された水
中ポンプ11の吐出管12にジエツトノズル1
3、デイストリビユーター14を内蔵したノツズ
ル管15をフランジ16で接続させ、更にジエツ
トノズル13、デイストリビユーター14の中間
にノツズル管15に屈曲自在の空気吸入管17を
配設してその他端を大気に開放し、更にノツズル
管15と螺旋羽根旋回流造流管18、可撓管接続
管19を夫々フランジ20,21で接続し、可撓
管接続管19、送水可撓管6を締結バンド22で
連結する。23は水中モーター用電線、24は空
気吸入管17を水面に浮上させるブイ、25は配
電盤、26は水底面、27は水表面を示す。
The device of this invention will be explained based on a drawing. A lower cone 4 is fastened to a float 1 floating on the water surface by a nozzle attachment band 2 and a fastening band 3, and a tripod support plate 5 is provided inside the lower end of the cone.
Then, the flexible water supply pipe 6 is fastened with a fastening band 10 to a truncated conical annular nozzle constituted by an upper cone 9 connected with a bolt and a nut 8, with the spacing adjusted by an adjustment spacer 7. A jet nozzle 1 is connected to the discharge pipe 12 of the submersible pump 11, which is also installed at the bottom of the water.
3. A nozzle pipe 15 containing a built-in distributor 14 is connected with a flange 16, and a bendable air suction pipe 17 is arranged in the nozzle pipe 15 between the jet nozzle 13 and the distributor 14, and the other end is connected. is opened to the atmosphere, and further, the nozzle pipe 15, the spiral vane swirling flow pipe 18, and the flexible pipe connecting pipe 19 are connected with flanges 20 and 21, respectively, and the flexible pipe connecting pipe 19 and the water supply flexible pipe 6 are connected with a fastening band. Connect with 22. 23 is an electric wire for an underwater motor, 24 is a buoy for floating the air suction pipe 17 to the water surface, 25 is a switchboard, 26 is a water bottom surface, and 27 is a water surface.

上述の如く構成された本考案装置の作用を説明
するに、此の装置は第7図の如く湖沼、貯水池、
養魚池等の曝気作用が最も効果的に作用する場所
を選んで水中に投下すると水中ポンプ11が重錘
として作用して水底面26に接地した位置におい
て設置された円錐形環状ノツズルはフロート1の
浮力により水表面27上に浮ぶ。此のとき円錐形
環状ノツズルはフロート1とともに水位の変化に
応じて送水可撓管6の屈曲伸縮により自動的に上
下に移動するため特別にその高さを調節する必要
はない。
To explain the operation of the device of the present invention configured as described above, this device can be used in lakes, reservoirs, etc. as shown in Figure 7.
When a place where the aeration effect is most effective, such as a fish pond, is selected and dropped into the water, the submersible pump 11 acts as a weight, and the conical annular nozzle installed at the position where it is grounded on the bottom surface 26 of the float 1. It floats on the water surface 27 due to buoyancy. At this time, the conical annular nozzle automatically moves up and down together with the float 1 by bending and expanding/contracting the flexible water pipe 6 in response to changes in the water level, so there is no need to specifically adjust its height.

次に水中モーター11を始動すると水域底部の
汚水、無酸素水を吸引し、之を上部吐出管12内
に吐出すると、ノツズル管15内のジエツトノズ
ル13より噴出しデイストリビユーター14に入
る際のアスピレーター作用により空気吸入管17
より大気を吸引し微細気泡が形成される。次に微
細気泡混合水が螺旋羽根旋回流造流管18内に入
り、管内の羽根車により旋回流を与えられつつ可
撓管接続管19を経て送水可撓管6内を第6図の
如く旋回しつつ上昇し、此の際の気液混合作用に
より充分に酸素を溶解して水面上の円錐形環状ノ
ツズルより朝顔状に空中に撒布され、飛散時にお
ける水滴と空気との接触、水面落下時の水滴によ
る水面の乱れ等を含めて優れた曝気効果を発揮し
撒布状態も旋回流による影響のため円周上均一と
なる。
Next, when the submersible motor 11 is started, the sewage and anoxic water at the bottom of the water body are sucked in, and when they are discharged into the upper discharge pipe 12, they are ejected from the jet nozzle 13 in the nozzle pipe 15, and when entering the distributor 14. Air suction pipe 17 due to aspirator action
More air is sucked in and fine bubbles are formed. Next, the fine bubble mixed water enters the spiral vane swirl flow pipe 18, and while being given a swirling flow by the impeller inside the pipe, it passes through the flexible pipe connection pipe 19 and swirls inside the water supply flexible pipe 6 as shown in Fig. 6. At this point, the gas-liquid mixing action sufficiently dissolves oxygen, and the conical annular nozzle on the water surface disperses it into the air in the shape of a morning glory. It exhibits an excellent aeration effect, including the turbulence of the water surface, and the distribution condition is uniform around the circumference due to the influence of the swirling flow.

本考案装置は上述の如く極めて簡単な構造であ
り、水質の保全及び改良にその曝気作用は有効に
してかつ大であるから工業上大なる効果がある。
As mentioned above, the device of the present invention has an extremely simple structure, and its aeration effect is effective and large in preserving and improving water quality, so it has great industrial effects.

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

第1図は本考案装置の縦断側面図、第2図は円
錐形環状ノツズルの縦断側面図及びA−A矢視断
面図、第3図はフロート及び円錐形環状ノツズル
の平面図、第4図は螺旋羽根旋回流造流管の縦断
側面図及び平面図、第5図はジエツトノツズル及
びデイストリビユーターを含むノツズル管の縦断
側面図及び平面図、第6図は作用説明図、第7図
は此の装置を水底に設置した状態を示す作用説明
図である。 1……フロート、2……ノツズル取付けバン
ド、3……締結バンド、4……下部円錐、5……
三脚支持板、6……送水可撓管、7……調整間
座、8……ボルト及びナツト、9……上部円錐、
10……締結バンド、11……水中ポンプ、12
……吐出管、13……ジエツトノツズル、14…
…デイストリビユーター、15……ノツズル管、
16……フランジ、17……空気吸入管、18…
…螺旋羽根旋回流造流管、19……可撓管接続
管、20……フランジ、21……フランジ、22
……締結バンド、23……水中モーター用電線、
24……ブイ、25……配電盤、26……水底
面、27……水表面。
Fig. 1 is a longitudinal side view of the device of the present invention, Fig. 2 is a longitudinal side view and a sectional view taken along the line A-A of the conical annular nozzle, Fig. 3 is a plan view of the float and the conical annular nozzle, and Fig. 4 5 is a longitudinal side view and a plan view of a nozzle tube including a jet nozzle and a distributor, FIG. 6 is an explanatory diagram of the function, and FIG. FIG. 3 is an explanatory view showing the operation of the device installed on the bottom of the water. 1... Float, 2... Knotzzle mounting band, 3... Fastening band, 4... Lower cone, 5...
Tripod support plate, 6... Flexible water pipe, 7... Adjustment spacer, 8... Bolt and nut, 9... Upper cone,
10... Fastening band, 11... Submersible pump, 12
...Discharge pipe, 13...Jet nozzle, 14...
... Distributor, 15... Nozzle tube,
16...flange, 17...air suction pipe, 18...
...Spiral vane swirl flow pipe, 19...Flexible pipe connection pipe, 20...Flange, 21...Flange, 22
... Fastening band, 23 ... Electric wire for underwater motor,
24...Buoy, 25...Switchboard, 26...Water bottom, 27...Water surface.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 水底に設置された水中ポンプの吐出口と、水面
に浮ぶ逆載頭円錐形環状ノツズルをジエツト空気
吸引装置、螺旋羽根管旋回流造流装置と屈曲自在
の送水可撓管で連接して、吸引汚水を送水中気液
混合しつつ環状ノツズルより朝顔状に空中に放射
撒布することを特徴とするジエツト吸気旋回流曝
気装置。
The discharge port of the submersible pump installed at the bottom of the water and the inverted conical annular nozzle floating on the water surface are connected by a jet air suction device, a spiral vane pipe swirling flow straightening device, and a flexible water supply pipe that can be bent freely to suck sewage. A jet intake swirl flow aeration device characterized in that the air is mixed with gas and liquid in the supplied water and is radiated into the air in a morning glory shape from an annular nozzle.
JP1982075756U 1982-05-25 1982-05-25 Jet intake swirl flow aerator Granted JPS58178396U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1982075756U JPS58178396U (en) 1982-05-25 1982-05-25 Jet intake swirl flow aerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1982075756U JPS58178396U (en) 1982-05-25 1982-05-25 Jet intake swirl flow aerator

Publications (2)

Publication Number Publication Date
JPS58178396U JPS58178396U (en) 1983-11-29
JPS638475Y2 true JPS638475Y2 (en) 1988-03-14

Family

ID=30085101

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1982075756U Granted JPS58178396U (en) 1982-05-25 1982-05-25 Jet intake swirl flow aerator

Country Status (1)

Country Link
JP (1) JPS58178396U (en)

Also Published As

Publication number Publication date
JPS58178396U (en) 1983-11-29

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