JP3156173B2 - Pressurized floating purification device - Google Patents

Pressurized floating purification device

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Publication number
JP3156173B2
JP3156173B2 JP34864795A JP34864795A JP3156173B2 JP 3156173 B2 JP3156173 B2 JP 3156173B2 JP 34864795 A JP34864795 A JP 34864795A JP 34864795 A JP34864795 A JP 34864795A JP 3156173 B2 JP3156173 B2 JP 3156173B2
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JP
Japan
Prior art keywords
water
tank
air
pressurized
pressurizing
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.)
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JP34864795A
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Japanese (ja)
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JPH09168777A (en
Inventor
浩史 山本
Original Assignee
株式会社山広
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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、例えば汚水中に空
気を加圧して溶解させ、その後この汚水を大気解放し
て、上記溶解した空気を微細気泡として取り出すことに
より、水中に酸素を溶解し水中の汚れをこの気泡と共に
浮上分離する加圧浮上浄化装置に関するものである。
The present invention relates to a method for dissolving oxygen in water by, for example, dissolving air by pressurizing air in sewage, releasing the sewage to the atmosphere, and taking out the dissolved air as fine bubbles. The present invention relates to a pressurized flotation purification device that flotates and separates dirt in water with these bubbles.

【0002】[0002]

【従来の技術】水処理を行うに際し、処理すべき水に大
量の微細気泡を発生させ、水とこの微細気泡を接触させ
て浮上分離を行う加圧浮上浄化法が一般に知られてい
る。
2. Description of the Related Art In carrying out water treatment, there is generally known a pressurized flotation purification method in which a large amount of fine bubbles are generated in water to be treated, and the fine bubbles are brought into contact with water to perform flotation separation.

【0003】上記加圧浮上浄化を行う装置としては、汲
み上げた水を密閉タンクに入れ、この密閉タンク内に3
〜5kg/cm2 の加圧空気を供給することによりこの
空気を水中に溶け込ませる一方、この空気を溶存した水
を大気開放することによりこの溶存した空気を微細気泡
となし、水中の汚れをこの微細気泡と共に取り出すもの
が周知である。
[0003] As an apparatus for purifying the pressure flotation, pumped water is put into a closed tank, and 3
By supplying pressurized air of about 5 kg / cm 2 , this air is dissolved in water, while the water in which this air is dissolved is released to the atmosphere to make the dissolved air fine bubbles, thereby removing dirt in the water. What is taken out together with fine bubbles is well known.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、上記従
来の加圧浮上浄化装置においては、加圧タンク内におけ
る攪拌混合効率が悪いことから空気の溶解効率が悪く、
その結果、微細気泡の発生量が減少することになり、浮
上分離能力の低下や排水に対する酸素の供給能力の低下
をまねく等の問題を有している。
However, in the above-mentioned conventional pressurized floating purification device, the efficiency of dissolving air is poor due to poor stirring and mixing efficiency in the pressurized tank.
As a result, the amount of generated fine bubbles is reduced, and there are problems such as a decrease in flotation separation capability and a decrease in oxygen supply capability to wastewater.

【0005】本発明は叙上の如き実状に対処し、加圧用
タンク中に渦流を発生させた状態でエアレーションを行
うことにより、上記空気の溶解効率を高め、これにより
上記水処理プラントを従来より小規模で低コストにする
ことを目的とするものである。
[0005] The present invention addresses the above-mentioned situation and improves the dissolving efficiency of the air by performing aeration in a state in which a vortex is generated in the pressurizing tank, thereby improving the water treatment plant. It is intended to be small and low cost.

【0006】[0006]

【課題を解決するための手段】すなわち、上記目的に適
合する本発明の加圧浮上浄化装置の特徴は、加圧ポンプ
等により汲み上げた水を加圧用タンクに入れ、このタン
ク内に加圧空気を供給することによりこの空気を水に溶
け込ませる一方、この水を大気解放することにより上記
溶存した空気を微細気泡となし、水中の汚れをこの気泡
と共に取り出す加圧浮上浄化装置において、上記加圧用
タンクを立直した筒状に形成すると共に、この加圧用タ
ンクの外周部上部に、液面の上方からタンクの接線方向
に水を噴射し、この噴射した水により上記タンク内に渦
流を発生させるノズル部を形成せしめたところにある。
That is, a feature of the pressure flotation purification apparatus of the present invention that meets the above-mentioned object is that water pumped by a pressure pump or the like is put into a tank for pressurization, and pressurized air is introduced into the tank. While the air is dissolved in water by supplying the air, the water is released to the atmosphere to form the dissolved air into fine bubbles, and the dirt in the water is removed together with the bubbles. A nozzle that forms a tank in an upright cylindrical shape and injects water in the tangential direction of the tank from above the liquid level to the upper part of the outer periphery of the pressurizing tank, and generates a vortex in the tank using the injected water. The part is formed.

【0007】また、上記本発明浄化装置において、この
タンクの略半径方向に延出された攪拌板を形成し、部分
的に渦流を阻止することによってさらに攪拌効果を高め
ることも可能であり、さらに上記ノズル部から噴射され
る水に対し、3kg/cm2〜5kg/cm2 の圧力で
加圧混合することも好適である。
Further, in the purifying apparatus of the present invention, it is possible to further increase the stirring effect by forming a stirring plate extending substantially in the radial direction of the tank and partially preventing a vortex. to the water ejected from the nozzle portion, it is also preferable to mix pressurized at a pressure of 3kg / cm 2 ~5kg / cm 2 .

【0008】[0008]

【作用】上記本発明の浄化装置においては、ノズル部か
ら水が、タンク上部の空気を巻き込みながらタンク内に
渦流を起こすように噴射されることから、水の深層まで
エアレーションを可能にして気泡の導入拡散効果を高
め、空気の溶解効率を従来に比し大幅に向上させること
ができ、これにより汚水中に高効率で酸素供給を行い、
大気開放時における水中の微細気泡の量を大きく増大さ
せることが可能となる。
In the purifying apparatus of the present invention, since the water is injected from the nozzle portion so as to cause a vortex into the tank while entraining the air in the upper part of the tank, it is possible to aerate to a deep layer of the water to form bubbles. The introduction and diffusion effect can be enhanced, and the dissolution efficiency of air can be greatly improved compared to the past, thereby supplying oxygen to wastewater with high efficiency,
This makes it possible to greatly increase the amount of microbubbles in water at the time of opening to the atmosphere.

【0009】[0009]

【実施例】以下さらに添付図面を参照して、本発明の実
施例を説明する。
Embodiments of the present invention will be described below with reference to the accompanying drawings.

【0010】図1は本発明実施例の加圧浮上浄化装置を
示すブロック図であり、図において1は処理前の水のプ
ール、2は減圧用タンク、3は加圧ポンプ、4は加圧用
タンク、5は処理後の水のプール、Sは制御盤を夫々示
している。
FIG. 1 is a block diagram showing a pressurized floating purification apparatus according to an embodiment of the present invention. In FIG. 1, 1 is a pool of water before treatment, 2 is a depressurizing tank, 3 is a pressurizing pump, and 4 is a pressurizing pump. The tank 5 is a pool of water after treatment, and S is a control panel.

【0011】上記減圧用タンク2は、このタンク2内の
水を減圧し、この水に予め溶解していた気体を脱気する
真空ポンプ6を備え、また減圧調整バルブ7、流量計
8、圧力センサー9、および水位センサー10を備えて
いる。
The depressurizing tank 2 includes a vacuum pump 6 for depressurizing the water in the tank 2 and degassing a gas previously dissolved in the water. A sensor 9 and a water level sensor 10 are provided.

【0012】上記減圧調整バルブ7は減圧タンク2内の
真空度を調整することにより、タンク2内で除去する気
体量や全体の流量調整を行う。また、上記真空ポンプ6
は上記タンク2の上部に溜まった気体を排出することに
より、空気(酸素)以上に溶解率の高い気体を水中から
除去し、次工程での空気の溶解率を高めることが可能で
ある。そして、上記水位センサー10は真空ポンプ6の
ON・OFF制御を行い、上記圧力センサー9はタンク
2内の真空度の計測と異常圧の検知を行う。
The pressure reducing valve 7 controls the amount of gas to be removed from the tank 2 and the overall flow rate by adjusting the degree of vacuum in the pressure reducing tank 2. The above vacuum pump 6
By discharging gas accumulated in the upper portion of the tank 2, gas having a higher dissolution rate than air (oxygen) can be removed from water, and the dissolution rate of air in the next step can be increased. The water level sensor 10 controls ON / OFF of the vacuum pump 6, and the pressure sensor 9 measures the degree of vacuum in the tank 2 and detects abnormal pressure.

【0013】一方、上記加圧用タンク3は、上記加圧ポ
ンプ3から続く流水口に形成されたノズル部11と、エ
アコンプレッサー12と、圧力センサー13と、水位セ
ンサー14とを備えている。また、この加圧用タンク4
の下部には、加圧された水をプール5に放出するための
圧力開放バルブ15と、ドレンを排出するための自動排
水弁16とが設けられている。
On the other hand, the pressurizing tank 3 includes a nozzle portion 11 formed at a water outlet following the pressurizing pump 3, an air compressor 12, a pressure sensor 13, and a water level sensor 14. Also, this pressurizing tank 4
A pressure release valve 15 for discharging pressurized water to the pool 5 and an automatic drainage valve 16 for discharging drain are provided at a lower portion of the pool.

【0014】上記ノズル部11は、円筒状に設けられた
上記加圧用タンク4の外周部付近に設置され、液面の上
方からタンク4の接線方向斜め下方に水を噴射し、この
噴射した水によりタンク4内の水に渦流を発生させるも
のである。この噴射される水は、前記加圧ポンプ3によ
って3kg/cm2 〜5kg/cm2 に加圧されてい
る。
The nozzle portion 11 is installed near the outer periphery of the pressurizing tank 4 provided in a cylindrical shape, and injects water from above the liquid level obliquely downward in the tangential direction of the tank 4. Thus, a vortex is generated in the water in the tank 4. Water is the injection is pressurized to 3kg / cm 2 ~5kg / cm 2 by the pressure pump 3.

【0015】そして、加圧用タンク4には、上記渦流に
直交するように3枚の攪拌板17がタンク4の外周部に
半径方向に固定されており、部分的に渦流の抵抗となる
ことによって攪拌効果を高めている。またさらに、上記
加圧用タンク4の中心には棒状の永久磁石18が、上を
N極、下をS極として設置されている。すなわち、ノズ
ル部11から噴射した水を上記磁石18を中心にタンク
4内で回転させることにより、水と空気が磁場の影響を
受けてさらに溶解し易くなる。
In the pressurizing tank 4, three agitating plates 17 are fixed radially to the outer peripheral portion of the tank 4 so as to be orthogonal to the vortex. Increases the stirring effect. Further, a rod-shaped permanent magnet 18 is installed at the center of the pressurizing tank 4 with an upper N pole and a lower S pole. That is, by rotating the water jetted from the nozzle portion 11 around the magnet 18 in the tank 4, the water and the air are more easily dissolved under the influence of the magnetic field.

【0016】これらノズル部11と攪拌板17では、ノ
ズル部11からタンク4上部の空気を巻き込みながらタ
ンク4内に渦流を起こすように噴射し、この渦流を上記
攪拌板17により混合する。すなわち、渦流と攪拌板1
7との併用により、他の動力を必要とせずに効率よく空
気と水の混合溶解を行うことが可能である。
In the nozzle section 11 and the stirring plate 17, the air in the upper portion of the tank 4 is jetted from the nozzle section 11 so as to generate a vortex into the tank 4 while being entrained, and the vortex is mixed by the stirring plate 17. That is, the vortex and the stirring plate 1
By using in combination with 7, it is possible to efficiently mix and dissolve air and water without requiring any other power.

【0017】また、上記エアコンプレッサー12は加圧
用タンク4内に加圧空気を送るものであり、上記水位セ
ンサー14は水位を検知して上記エアコンプレッサー1
2のON・OFF制御を行う。そして、圧力センサー1
3は圧力を計測して異常圧の有無を検知し、上記自動排
水弁16は定期的に排水することにより、加圧用タンク
4中の異物の付着防止を図ると共に、ゴミ等を排出する
機能を有している。
The air compressor 12 sends pressurized air into the pressurizing tank 4, and the water level sensor 14 detects a water level to detect the water level.
2 ON / OFF control is performed. And pressure sensor 1
The automatic drain valve 16 measures the pressure to detect the presence or absence of abnormal pressure, and the automatic drain valve 16 periodically drains the water to prevent adhesion of foreign matter in the pressurizing tank 4 and discharge dust and the like. Have.

【0018】さらに前記圧力開放バルブ15は、空気を
高濃度に溶解した加圧水を加圧用タンク4からプール5
に開放することにより、上記溶存酸素の多い加圧水から
上記プール5内で微細気泡を発生させる。
Further, the pressure release valve 15 supplies pressurized water in which air is dissolved at a high concentration from the pressurizing tank 4 to the pool 5.
To generate fine bubbles in the pool 5 from the pressurized water having a large amount of dissolved oxygen.

【0019】最後に、前記制御盤Sはタイマーにより、
加圧ポンプ3、真空ポンプ6、エアコンプレッサー1
2、および自動排水弁16の自動運転とON・OFF制
御を行う。また、各圧力センサー9、13は、各タンク
2、4で夫々異常圧力を検知した際に装置全体の運転を
自動停止させる。
Finally, the control panel S is operated by a timer.
Pressurizing pump 3, vacuum pump 6, air compressor 1
2. Automatic operation and ON / OFF control of the automatic drain valve 16 are performed. The pressure sensors 9 and 13 automatically stop the operation of the entire apparatus when abnormal pressures are detected in the tanks 2 and 4, respectively.

【0020】しかして、上記本発明実施例の加圧浮上浄
化装置では、先ず減圧用タンク2において200〜70
0mmHgの真空度で減圧脱気をすることにより、水中
に溶解していた気体を除去する。気体分子は水の分子の
隙間に入っていると考えられているが、従来の加圧・曝
気程度では、先に溶けている気体分子を押し出して、こ
の隙間に酸素等を入れようとするために効率が悪い。例
えば、水に溶解する比率で、酸素を1とすればアンモニ
アは3000である。
In the pressurized levitation purifying apparatus according to the embodiment of the present invention, first, 200 to 70
The gas dissolved in the water is removed by degassing under reduced pressure at a degree of vacuum of 0 mmHg. It is thought that gas molecules are in gaps between water molecules, but with conventional pressure / aeration, gas molecules that are dissolved first are pushed out and oxygen or the like is put into this gap. Inefficient. For example, if oxygen is 1 in a ratio of dissolving in water, ammonia is 3000.

【0021】次に上記脱気後の水に加圧して空気と混合
する。この場合、ヘンリーの法則により圧力下で気体は
液体に溶け易いというところから、脱気から加圧という
工程では、従来を大きく越える高効率で水中の溶存酸素
量を増大させることが可能である。この場合、前記ノズ
ル部11による渦流と攪拌板17とを利用して、加圧用
タンク4内で水と空気を混合することにより、上記水中
の溶存酸素量をさらに効率よく増大させることが可能で
ある。
Next, the deaerated water is pressurized and mixed with air. In this case, since the gas is easily dissolved in the liquid under pressure according to Henry's law, in the process of degassing to pressurizing, it is possible to increase the amount of dissolved oxygen in the water with high efficiency which is much higher than the conventional one. In this case, by mixing water and air in the pressurizing tank 4 by using the vortex generated by the nozzle portion 11 and the stirring plate 17, the amount of dissolved oxygen in the water can be more efficiently increased. is there.

【0022】ちなみに、脱気により空気の溶解効率が高
まると、通常加圧タンク4内での水の滞留時間が1.5
〜2分とされているのに対し、時間短縮と加圧タンク4
の小型化を図ることができる。また、加圧力も通常は3
〜5kg/cm2 といわれているが、それよりも低圧化
することが可能となる。なお、上記工程において、加圧
用タンク4内の水位を検知することによってエアコンプ
レッサー12をON・OFFさせれば、空気の溶解する
量を調整する必要はなくなり、開放バルブ開閉による圧
力の調整にも影響されずに、加圧ポンプ3の能力内で任
意に圧力設定が可能である。
By the way, when the efficiency of dissolving air is increased by degassing, the residence time of water in the pressurized tank 4 is usually 1.5 times.
22 minutes, the time is reduced and the pressure tank 4
Can be reduced in size. Also, the pressure is usually 3
It is said to be 55 kg / cm 2 , but it is possible to lower the pressure. In the above process, if the air compressor 12 is turned ON / OFF by detecting the water level in the pressurizing tank 4, it is not necessary to adjust the amount of dissolved air, and the pressure can be adjusted by opening and closing the open valve. The pressure can be arbitrarily set within the capacity of the pressure pump 3 without being affected.

【0023】そして、上記加圧用タンク4の圧力開放バ
ルブ15を開き、加圧水をプール5に開放することによ
り、水中に大量の微細気泡が発生し、この気泡の浮上と
共に汚れを浮上分離させることによって、水からこの汚
れを除去することが可能となる。
By opening the pressure release valve 15 of the pressurizing tank 4 and releasing the pressurized water to the pool 5, a large amount of fine bubbles are generated in the water, and the dirt floats and separates with the floating of the bubbles. This makes it possible to remove this dirt from the water.

【0024】以上、本発明の実施例を説明したが、前記
減圧用タンク2は、実施例の如く独立して設ける以外
に、加圧用タンク4と兼用するように構成することも可
能である。また、減圧用タンク2に必要に応じ、脱気し
た気体の消臭を行う消臭機19を付設すると共に、プー
ル1のダクトに逆止弁20を付設することも好適であ
る。
While the embodiment of the present invention has been described above, the depressurizing tank 2 may be configured to also serve as the pressurizing tank 4 in addition to being provided independently as in the embodiment. It is also preferable to attach a deodorizer 19 for deodorizing the degassed gas to the depressurizing tank 2 as necessary, and to attach a check valve 20 to the duct of the pool 1 if necessary.

【0025】[0025]

【発明の効果】以上説明したように、本発明の加圧浮上
浄化装置は、空気加圧用のタンクを立直した筒状に形成
すると共に、この加圧用タンクの外周部上部に、液面の
上方からタンクの接線方向に水を噴射し、この噴射した
水により上記タンク内に渦流を発生させるノズル部を形
成せしめたものであり、ノズル部から水が、タンク上部
の空気を巻き込みながらタンク内に渦流を起こすように
噴射されることから、水の深層までエアレーションを可
能にして気泡の導入拡散効果を高め、空気の溶解効率を
従来に比し大幅に向上させ、これにより汚水中に高効率
で酸素供給を行い、大気開放時の微細気泡の量を増大せ
しめて汚れの回収率を向上させ、その結果、従来のシス
テムより小規模で低コストの水処理プラントを提供する
との顕著な効果を奏するものである。
As described above, the pressurized floating purification device of the present invention has an air pressurizing tank formed in an upright cylindrical shape, and an upper portion of the outer peripheral portion of the pressurizing tank is provided with an upper liquid level. From the tank in the tangential direction of the tank, and the injected water forms a nozzle that generates a vortex in the tank.Water from the nozzle into the tank while entraining the air above the tank Injected so as to create a vortex, it enables aeration to the deep layer of water and enhances the effect of introducing and diffusing air bubbles, greatly improving the dissolution efficiency of air compared to the past, and thereby enabling high efficiency in wastewater By supplying oxygen and increasing the amount of microbubbles at the time of opening to the atmosphere, the recovery rate of dirt is improved, and as a result, the remarkable effect of providing a smaller and lower cost water treatment plant than the conventional system is achieved. It is intended to.

【0026】さらに、上記渦流と攪拌板とを併用するこ
とにより、他の動力を必要とすることなく、さらに効率
よく上記水と空気の混合を行わしめることが可能であ
る。
Further, by using the vortex and the stirring plate together, it is possible to more efficiently mix the water and the air without requiring any other power.

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

【図1】本発明実施例の加圧浮上浄化装置を示すブロッ
ク図である。
FIG. 1 is a block diagram showing a pressure flotation purification apparatus according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 プール 2 減圧用タンク 3 加圧ポンプ 4 加圧用タンク 5 プール 6 真空ポンプ 7 減圧調整バルブ 8 流量計 9 圧力センサー 10 水位センサー 11 ノズル部 12 エアコンプレッサー 13 圧力センサー 14 水位センサー 15 圧力開放バルブ 16 自動排水弁 17 攪拌板 18 永久磁石 19 消臭機 20 逆止弁 DESCRIPTION OF SYMBOLS 1 Pool 2 Decompression tank 3 Pressure pump 4 Pressure tank 5 Pool 6 Vacuum pump 7 Pressure reduction valve 8 Flow meter 9 Pressure sensor 10 Water level sensor 11 Nozzle part 12 Air compressor 13 Pressure sensor 14 Water level sensor 15 Pressure release valve 16 Automatic Drain valve 17 Stir plate 18 Permanent magnet 19 Deodorizer 20 Check valve

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 加圧ポンプ等により汲み上げた水を加圧
用タンクに入れ、このタンク内に加圧空気を供給するこ
とによりこの空気を水に溶け込ませる一方、この水を大
気解放することにより上記溶存した空気を微細気泡とな
し、水中の汚れをこの気泡と共に取り出す加圧浮上浄化
装置において、上記加圧用タンクを立直した筒状に形成
すると共に、この加圧用タンクの外周部上部に、液面の
上方からタンクの接線方向に水を噴射し、この噴射した
水により上記タンク内に渦流を発生させるノズル部を形
成せしめたことを特徴とする加圧浮上浄化装置。
1. The water pumped by a pressurizing pump or the like is put into a pressurizing tank, and pressurized air is supplied into the tank to dissolve the air in the water, while releasing the water to the atmosphere. In a pressurized flotation purification device for forming dissolved air into fine air bubbles and removing dirt in water together with the air bubbles, the pressurizing tank is formed in an upright cylindrical shape, and a liquid level is formed on an upper peripheral portion of the pressurizing tank. A pressurized flotation purification apparatus characterized in that water is jetted from above the tank in a tangential direction of the tank, and a nozzle portion for generating a vortex in the tank is formed by the jetted water.
【請求項2】 上記加圧用タンク内に、このタンクの略
半径方向に延出された攪拌板を形成した請求項1記載の
加圧浮上浄化装置。
2. The pressurized flotation purification device according to claim 1, wherein a stirring plate extending in a substantially radial direction of the tank is formed in the pressurizing tank.
【請求項3】 上記ノズル部から噴射される水に対し、
3kg/cm2 〜5kg/cm2 の圧力を加圧した請求
項1または2記載の加圧浮上浄化装置。
3. The water jetted from the nozzle portion,
3kg / cm 2 ~5kg / cm floatation on purification system of a pressurized claim 1 or 2, wherein a pressure of 2.
JP34864795A 1995-12-18 1995-12-18 Pressurized floating purification device Expired - Lifetime JP3156173B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34864795A JP3156173B2 (en) 1995-12-18 1995-12-18 Pressurized floating purification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34864795A JP3156173B2 (en) 1995-12-18 1995-12-18 Pressurized floating purification device

Publications (2)

Publication Number Publication Date
JPH09168777A JPH09168777A (en) 1997-06-30
JP3156173B2 true JP3156173B2 (en) 2001-04-16

Family

ID=18398414

Family Applications (1)

Application Number Title Priority Date Filing Date
JP34864795A Expired - Lifetime JP3156173B2 (en) 1995-12-18 1995-12-18 Pressurized floating purification device

Country Status (1)

Country Link
JP (1) JP3156173B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6488853B1 (en) * 2000-10-04 2002-12-03 Great Circle Technologies, Inc. Process and apparatus for treating wastewater
KR101336169B1 (en) * 2013-07-22 2013-12-03 주식회사 동신이엔텍 Water purifying apparatus using sedimentation and dissolved air flotation

Also Published As

Publication number Publication date
JPH09168777A (en) 1997-06-30

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