JP2006075765A - Scum removal method - Google Patents

Scum removal method Download PDF

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JP2006075765A
JP2006075765A JP2004263883A JP2004263883A JP2006075765A JP 2006075765 A JP2006075765 A JP 2006075765A JP 2004263883 A JP2004263883 A JP 2004263883A JP 2004263883 A JP2004263883 A JP 2004263883A JP 2006075765 A JP2006075765 A JP 2006075765A
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Prior art keywords
scum
tank
mixed liquid
skimmer
concentration
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Takanobu Kashiuchi
孝信 樫内
Tadafusa Uchida
只房 内田
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Shimizu Construction Co Ltd
Shimizu Corp
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Shimizu Construction Co Ltd
Shimizu Corp
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    • 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

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for removing scum by withdrawing it, where the scum is generated at an aerator, or the like, during waste water treatment with activated sludge and the method by which the concentration of the scum in mixed liquid containing the scum and activated sludge can be increased, and the efficiency of scum removal can be increased as a result. <P>SOLUTION: A scum removal apparatus is used which is provided with: a scum skimmer 2 for sucking the mixed liquid containing the scum and activated sludge floating in the vicinity of the water surface in a water treating tank; a force-feeding means 4 for force-feeding the mixed liquid sucked from the scum skimmer 2; and a scum concentrating tank 1 for temporarily storing the mixed liquid force-fed by the force-feeding means 4 and further returning the same to the water treating tank. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

この発明は、活性汚泥によって廃水を処理する際に発生するスカムを効率よく除去できるスカムの除去方法およびその装置ならびにこのスカム除去装置を備えた廃水処理装置に関する。   The present invention relates to a scum removal method and apparatus capable of efficiently removing scum generated when wastewater is treated with activated sludge, and a wastewater treatment apparatus equipped with the scum removal apparatus.

廃水を活性汚泥法により浄化処理する際、食品工場などから排出される油脂分が多く含まれている廃水などを処理対象とする場合には、処理水中に放線菌が発生することが多々ある。この放線菌は、曝気によって生じた気泡に付着し、スカムを生成する。このスカムは曝気槽などから溢れるなどの障害を起こす。   When purifying wastewater by the activated sludge method, actinomycetes are often generated in the treated water when wastewater containing a large amount of oil and fat discharged from a food factory or the like is to be treated. This actinomycete adheres to bubbles generated by aeration and generates scum. This scum causes problems such as overflow from the aeration tank.

従来、このスカムの発生を防止するために、薬品による放線菌の殺菌、曝気量の調整などの方策が取られているが、その効果は不十分であった。
このため、一旦発生したスカムを除去すると言う対症療法的な方策が取られており、各種スカムスキマー、スカムポンプなどを用いてスカムを除去する方法が採用されている(特許文献1参照)。
Conventionally, in order to prevent the occurrence of this scum, measures such as sterilization of actinomycetes with chemicals and adjustment of the amount of aeration have been taken, but the effect has been insufficient.
For this reason, a symptomatic measure of removing once generated scum has been taken, and a method of removing scum using various scum skimmers, scum pumps, etc. is employed (see Patent Document 1).

しかしながら、スカムスキマーやスカムポンプを用いるものでは、スカムと活性汚泥を含む混合液を引き抜くため、引抜液のスカム濃度が低く、スカムの除去効率が低い欠点があった。このため、この引抜液を脱水処理する際の効率も悪いと言う欠点もある。
特開平10−216410号公報
However, those using a scum skimmer or scum pump have the disadvantages that the liquid mixture containing scum and activated sludge is drawn out, so that the scum concentration of the drawn liquid is low and the scum removal efficiency is low. For this reason, there also exists a fault that the efficiency at the time of dehydrating this drawing liquid is also bad.
JP-A-10-216410

よって、本発明における課題は、活性汚泥によって廃水処理を行う際、曝気槽などで発生するスカムを引き抜くことにより除去する方法において、スカムと活性汚泥を含む混合液中のスカム濃度を高めることができ、スカム除去効率を高めることができるようにすることにある。   Therefore, the problem in the present invention is to increase the scum concentration in a mixed liquid containing scum and activated sludge in a method of removing scum generated in an aeration tank or the like when performing wastewater treatment with activated sludge. It is to be able to increase the scum removal efficiency.

かかる課題を解決するため、
請求項1にかかる発明は、水処理槽の水面付近に浮遊しているスカムと活性汚泥とを含む混合液をスカムスキマーで吸入し、この混合液をスカム濃縮槽に送り、さらにこの混合液とスカムをスカムスキマーで再度吸入することを繰り返すことによりスカム濃縮槽での混合液中のスカム濃度を高め、このスカム濃縮槽のスカム濃度の高い混合液を引き抜くことを特徴とするスカムの除去方法である。
請求項2にかかる発明は、スカム濃縮槽からのスカム濃度の高い混合液を脱水処理することを特徴とする請求項1記載のスカムの除去方法である。
To solve this problem,
According to the first aspect of the present invention, a mixed liquid containing scum and activated sludge floating near the water surface of the water treatment tank is sucked by a scum skimmer, and the mixed liquid is sent to the scum concentrating tank. A scum removal method characterized by increasing the scum concentration in the liquid mixture in the scum concentration tank by repeatedly sucking the scum again with the scum skimmer and drawing out the liquid mixture having a high scum concentration in the scum concentration tank. is there.
The invention according to claim 2 is the scum removal method according to claim 1, characterized in that the liquid mixture having a high scum concentration from the scum concentration tank is dehydrated.

請求項3にかかる発明は、水処理槽の水面付近に浮遊するスカムと活性汚泥とを含む混合液を吸入するスカムスキマーと、このスカムスキマーから吸入された混合液を圧送する圧送手段と、この圧送手段で圧送された混合液を一時的に貯留し、この混合液の一部を上記水処理槽に戻し、残部をスカムスキマーに吸入させるスカム濃縮槽を備えたことを特徴とするスカムの除去装置である。
請求項4にかかる発明は、スカム濃縮槽から混合液を引き抜き、この混合液を脱水処理する脱水処理装置をさらに備えた請求項3記載のスカムの除去装置である。
According to a third aspect of the present invention, there is provided a scum skimmer for sucking a mixed liquid containing scum and activated sludge floating near the water surface of a water treatment tank, a pressure feeding means for pumping the mixed liquid sucked from the scum skimmer, A scum removal characterized by comprising a scum concentrating tank that temporarily stores the liquid mixture pumped by the pressure feeding means, returns a part of the liquid mixture to the water treatment tank, and sucks the remainder into the scum skimmer. Device.
The invention according to claim 4 is the scum removing device according to claim 3, further comprising a dehydration processing device for extracting the mixed solution from the scum concentration tank and dehydrating the mixed solution.

請求項5にかかる発明は、請求項3または4記載のスカムの除去装置が水処理槽内に設置されたことを特徴とする廃水処理装置である。   A fifth aspect of the present invention is a wastewater treatment apparatus in which the scum removing device according to the third or fourth aspect is installed in a water treatment tank.

本発明によれば、スカム濃縮槽における混合液中のスカム濃度が徐々に上昇する。このため、このスカム濃度の高い混合液を抜液すれば効率的にスカムの除去が行える。したがって、水処理槽でのスカムによる障害を予防することができる。さらに、高濃度のスカムと汚泥が抜液することができるので、このものの処分が容易になり、処理費用も安価となる。   According to the present invention, the scum concentration in the liquid mixture in the scum concentration tank gradually increases. Therefore, the scum can be efficiently removed by discharging the liquid mixture having a high scum concentration. Therefore, the failure | damage by the scum in a water treatment tank can be prevented. Furthermore, since high-concentration scum and sludge can be drained, the disposal of this product becomes easy and the processing cost is also low.

図1および図2は、本発明のスカム除去装置の一例を示すものである。
これらの図中において、符号101は、スカム除去装置を示す。このスカム除去装置101は、図示しない水処理槽、例えば曝気槽などの水面付近に設けられている。
そして、このスカム除去装置101は、スカム濃縮槽1と、スカムスキマー2と、圧送手段として機能する空気圧入パイプ4とから概略構成されている。上記スカム濃縮槽1は、さらに前槽11と中間槽12と後槽13とから構成されている。
前槽11には、スカムスキマー2が設けられている。このスカムスキマー2には、例えば市販のフロート式スカムスキマーをそのまま用いることができる。
1 and 2 show an example of the scum removing device of the present invention.
In these drawings, reference numeral 101 denotes a scum removing device. The scum removing device 101 is provided in the vicinity of the water surface of a water treatment tank (not shown) such as an aeration tank.
The scum removing device 101 is generally composed of a scum concentrating tank 1, a scum skimmer 2, and a pneumatic inlet pipe 4 that functions as a pressure feeding means. The scum concentration tank 1 further includes a front tank 11, an intermediate tank 12, and a rear tank 13.
A scum skimmer 2 is provided in the front tank 11. As this scum skimmer 2, for example, a commercially available float scum skimmer can be used as it is.

この例でのスカムスキマー2は、図2に示すように、2個のフロート21、21と1本のスカム吸入パイプ22とからなり、スカム吸入パイプ22の開口部付近の両側に2個のフロート21、21が取り付けられたものである。
このスカムスキマー2は、そのフロート21、21内に砂、水などの錘を入れることにより、水面上に浮上し、かつスカム吸入パイプ22の開口部が水面よりも若干沈んだ状態となるようになっている。
As shown in FIG. 2, the scum skimmer 2 in this example includes two floats 21 and 21 and one scum suction pipe 22, and two floats on both sides near the opening of the scum suction pipe 22. 21 and 21 are attached.
The scum skimmer 2 floats on the water surface by placing a weight such as sand or water in the floats 21 and 21 so that the opening of the scum suction pipe 22 is slightly submerged than the water surface. It has become.

このスカムスキマー2のスカム吸入パイプ22の下部は、前槽11の底部を貫通して下方に延び、その下部が連通パイプ3の一端側に移動可能に挿入されており、これによりスカム吸入パイプ22の水位の変動による上下方向の動きが許容されるようになっている。
この連通パイプ3は、U字状になっており、その立ち上がり部分の端部が後槽13の底部に開口している。
The lower portion of the scum suction pipe 22 of the scum skimmer 2 extends downward through the bottom of the front tank 11, and the lower portion is movably inserted into one end side of the communication pipe 3. The vertical movement due to the fluctuation of the water level is allowed.
The communication pipe 3 is U-shaped, and an end portion of the rising portion is open to the bottom of the rear tank 13.

また、連通パイプ3の立ち上がり部分には、空気圧入パイプ4が接続されており、この空気圧入パイプ4から空気が連通パイプ3内の混合液に吹き込まれ、これによって、図示するような混合液の流れ、すなわちスカム吸入パイプ22から吸い込まれた混合液が連通パイプ3を経て後槽13に流れ込む流れが形成されるようになっている。この空気圧入パイプ4からの空気の圧入が、この例での圧送手段となっている。
なお、空気圧入パイプ4を設けずに、通常のポンプを連通パイプ3に取り付け、これによって上述の混合液の流れを作るようにしてもよい。
Also, a pneumatic input pipe 4 is connected to the rising portion of the communication pipe 3, and air is blown into the mixed liquid in the communication pipe 3 from the pneumatic input pipe 4. A flow, that is, a flow in which the mixed solution sucked from the scum suction pipe 22 flows into the rear tank 13 through the communication pipe 3 is formed. The press-fitting of air from the pneumatic fitting pipe 4 is a pressure feeding means in this example.
In addition, without providing the pneumatic inlet pipe 4, a normal pump may be attached to the communication pipe 3 to create the above-described mixed liquid flow.

上記後槽13は、その満水位が他の前槽11および中間槽12の満水位よりも高くなるように構成されており、後槽13からの混合液が中間槽12に溢流するようになっている。
上記中間槽12は、前槽11と隔壁14で仕切られており、混合液がこの隔壁14の下部をくぐって中間槽12から前槽11に流れ込むようになっている。
The said rear tank 13 is comprised so that the full water level may become higher than the full water level of the other front tank 11 and the intermediate tank 12, so that the liquid mixture from the rear tank 13 may overflow into the intermediate tank 12. It has become.
The intermediate tank 12 is partitioned by a front tank 11 and a partition wall 14, and the mixed liquid flows into the front tank 11 from the intermediate tank 12 through the lower part of the partition wall 14.

また、中間槽12には、抜液パイプ5の一端が混合液中にその開口を臨ませた状態で設けられている。この抜液パイプ5は、ポンプ51に接続され、中間槽12内の混合液を引き抜き、図示しない脱水処理装置に送るようになっている。
また、中間槽12には、上記ポンプの動作を制御する水位スイッチ(図示略)が設けられている。
The intermediate tank 12 is provided with one end of the drainage pipe 5 facing the opening in the mixed liquid. The drainage pipe 5 is connected to a pump 51 to draw out the mixed liquid in the intermediate tank 12 and send it to a dehydration processing apparatus (not shown).
Further, the intermediate tank 12 is provided with a water level switch (not shown) for controlling the operation of the pump.

上記前槽11には、図2に示すように、上記スカムスキマー2のフロート21、21の浮遊を阻止するフロートふれ止め板15が取り付けられている。また、前槽11の前部には、壁部16が設けられている。この壁部16は、その高さが水処理槽の水位よりも低くされ、前槽11からの混合液がこの壁部16の上部を乗り越えて水処理槽に流れ込むようになっている。
そして、このようなスカム除去装置は、図1に示すように、水処理槽の水位Wに比べて、前槽11の壁部16の上端部の位置が低くなるように、水処理槽内に配設されている。
As shown in FIG. 2, the front tank 11 is provided with a float anti-skid plate 15 that prevents the floats 21 and 21 of the scum skimmer 2 from floating. Further, a wall portion 16 is provided at the front portion of the front tank 11. The height of the wall portion 16 is set lower than the water level of the water treatment tank, and the mixed liquid from the front tank 11 passes over the upper portion of the wall portion 16 and flows into the water treatment tank.
And, as shown in FIG. 1, such a scum removing device is provided in the water treatment tank so that the position of the upper end of the wall portion 16 of the front tank 11 is lower than the water level W of the water treatment tank. It is arranged.

このような構造のスカム除去装置にあっては、水処理槽から前槽11に流入した混合液のうち、水面に浮上するスカムと活性汚泥を含む混合液がスカムスキマー2のスカム吸入パイプ22から吸入され、連通パイプ3を通り、後槽13に流入する。この混合液は、さらに後槽13から溢流して中間槽12に流入し、ここから隔壁14をくぐって前槽11に流入し、その一部は水処理槽から新たに流入するスカムとともに再びスカムスキマー2に吸入される。また、その残部は、前槽11の壁部16を乗り越えて水処理槽に流れ出ることになる。   In the scum removing device having such a structure, of the mixed liquid flowing into the front tank 11 from the water treatment tank, the mixed liquid containing scum and activated sludge that floats on the water surface is supplied from the scum suction pipe 22 of the scum skimmer 2. It is sucked and passes through the communication pipe 3 and flows into the rear tank 13. This mixed liquid further overflows from the rear tank 13 and flows into the intermediate tank 12, then enters the front tank 11 through the partition wall 14, and part of the mixed liquid is again scumed together with the scum that newly flows from the water treatment tank. Inhaled by skimmer 2. Moreover, the remaining part will get over the wall part 16 of the front tank 11, and will flow out to a water treatment tank.

そして、このような混合液の循環を連続または断続して続けることにより、中間槽12における混合液中のスカム濃度が徐々に高くなる。すなわち、後槽13から溢流して中間槽12に流入したスカムを含む混合液は、隔壁14をくぐって前槽11に流入し、再び水面上のスカムとともにスカムスキマー2に吸入されるため、スカム濃度が上昇する。この動作が繰り返されることで、混合液中のスカム濃度が徐々に上昇し、中間槽12においてスカムが濃縮されることになる。
中間槽12のスカム濃度が高くなった混合液は、抜液パイプ5から引き抜かれ、脱水処理される。
このようにして、水処理槽のスカムが除去されることになる。
And by continuing the circulation of such a liquid mixture continuously or intermittently, the scum density | concentration in the liquid mixture in the intermediate tank 12 becomes high gradually. That is, the mixed liquid containing scum overflowing from the rear tank 13 and flowing into the intermediate tank 12 passes through the partition wall 14 and flows into the front tank 11 and is sucked into the scum skimmer 2 together with the scum on the water surface. Concentration increases. By repeating this operation, the scum concentration in the mixed liquid gradually increases, and the scum is concentrated in the intermediate tank 12.
The mixed liquid having a high scum concentration in the intermediate tank 12 is drawn out from the drain pipe 5 and dehydrated.
In this way, the scum of the water treatment tank is removed.

このようなスカム除去装置は、廃水処理装置を構成する水処理槽、例えば、曝気槽、沈殿槽などの内部の水面に近い位置に図1に示した水位Wとなるように設置されて使用に供される。
図3は、図1および図2に示したスカム除去装置を廃水処理装置の曝気槽(水処理槽)に設置した例を示すものである。
Such a scum removing device is installed and used at a position close to the water surface inside a water treatment tank constituting the waste water treatment apparatus, such as an aeration tank or a sedimentation tank, so that the water level W shown in FIG. Provided.
FIG. 3 shows an example in which the scum removing device shown in FIGS. 1 and 2 is installed in an aeration tank (water treatment tank) of a wastewater treatment apparatus.

図3において、処理原水は、調整槽31に送られ、ここで水量が調整されたのち、ポンプ32により第1流動床33に送られる。この第1流動床33では、多孔質担体に活性汚泥を担持したものを用いて処理が行われる。第1流動床33からの処理水は第2流動床34に送られ、同様の処理を受けた後、第1曝気槽35に溢流し、ここで曝気されて活性汚泥による処理を受ける。   In FIG. 3, the treated raw water is sent to the adjustment tank 31, and after the amount of water is adjusted here, it is sent to the first fluidized bed 33 by the pump 32. In the first fluidized bed 33, the treatment is performed using a porous carrier carrying activated sludge. The treated water from the first fluidized bed 33 is sent to the second fluidized bed 34 and subjected to the same treatment, and then overflows into the first aeration tank 35 where it is aerated and treated with activated sludge.

この第1曝気槽35には上述のスカム除去装置36が設置され、先に述べた動作が行われ、第1曝気槽35において発生したスカムが除去される。
第1曝気槽35からの廃水は、第2曝気槽37に送られ、同様の曝気処理を受けた後、ポンプにより液中膜槽38に送られる。
The first aeration tank 35 is provided with the scum removing device 36 described above, and the above-described operation is performed to remove the scum generated in the first aeration tank 35.
Waste water from the first aeration tank 35 is sent to the second aeration tank 37, and after receiving the same aeration process, it is sent to the submerged film tank 38 by a pump.

液中膜槽38は、分離膜を用い、ここに流入した廃水を濾過し、汚泥等と処理水とに分離するもので、分離された処理水は、外部に送られる。汚泥等は、ポンプで汚泥貯槽39に送られ、一旦貯留される。
汚泥貯槽39の汚泥は、さらにポンプで抜き出され、凝集混和槽40に送られ、ここでPAC、高分子凝集剤などの凝集剤が添加されて凝集される。
凝集された固形分は脱水機41によって脱水され、脱水ケーキとなって外部に排出される。
The submerged membrane tank 38 uses a separation membrane, filters waste water flowing into the submerged membrane tank 38 and separates it into sludge and the like, and the treated water is sent to the outside. Sludge and the like are sent to the sludge storage tank 39 by a pump and temporarily stored.
The sludge in the sludge storage tank 39 is further extracted by a pump and sent to the agglomeration and mixing tank 40, where a flocculating agent such as PAC or polymer flocculant is added and agglomerated.
The agglomerated solid content is dehydrated by the dehydrator 41 and discharged to the outside as a dehydrated cake.

また、この例では、スカム除去装置36のスカム濃度の高い混合液が抜液パイプ5を経て凝集混和槽40に送られ、汚泥貯槽39からの汚泥と同様にして脱水処理されるようになっている。   Further, in this example, the liquid mixture having a high scum concentration of the scum removing device 36 is sent to the agglomeration mixing tank 40 through the drain pipe 5 and dehydrated in the same manner as the sludge from the sludge storage tank 39. Yes.

このような廃水処理装置では、第1曝気槽35で発生したスカムがスカム除去装置36によって除去されるため、後段の第2曝気槽36以降の各処理槽に流入することがなく、これらの処理槽がスカムによる障害を受けることがなくなる。   In such a wastewater treatment apparatus, since the scum generated in the first aeration tank 35 is removed by the scum removal apparatus 36, these treatments do not flow into the treatment tanks after the second aeration tank 36 in the subsequent stage. The tank will not be damaged by scum.

本発明にあっては、スカム除去装置を設置する処理槽は、図3に示した第1曝気槽に限られることはなく、スカムが発生する恐れがある沈殿槽、原水槽、油分分離槽などに設置することができる。   In the present invention, the processing tank in which the scum removing device is installed is not limited to the first aeration tank shown in FIG. 3, but a precipitation tank, a raw water tank, an oil separation tank, or the like that may cause scum. Can be installed.

本発明のスカム除去装置の一例を示す概略断面図である。It is a schematic sectional drawing which shows an example of the scum removal apparatus of this invention. 図1に示したスカム除去装置の概略平面図である。FIG. 2 is a schematic plan view of the scum removing device shown in FIG. 1. 本発明のスカム除去装置を取り付けた廃水処理装置の例を示す概略構成図である。It is a schematic block diagram which shows the example of the waste water treatment apparatus which attached the scum removal apparatus of this invention.

符号の説明Explanation of symbols

1・・・スカム濃縮槽、2・・・スカムスキマー、3・・・連通パイプ、4・・・空気導入パイプ、40・・・凝集混和槽、41・・・脱水機
DESCRIPTION OF SYMBOLS 1 ... Scum thickening tank, 2 ... Scum skimmer, 3 ... Communication pipe, 4 ... Air introduction pipe, 40 ... Coagulation mixing tank, 41 ... Dehydrator

Claims (5)

水処理槽の水面付近に浮遊しているスカムと活性汚泥とを含む混合液をスカムスキマーで吸入し、この混合液をスカム濃縮槽に送り、さらにこの混合液とスカムをスカムスキマーで再度吸入することを繰り返すことによりスカム濃縮槽での混合液中のスカム濃度を高め、このスカム濃縮槽のスカム濃度の高い混合液を引き抜くことを特徴とするスカムの除去方法。   A mixed solution containing scum and activated sludge floating near the water surface of the water treatment tank is sucked by the scum skimmer, this mixed liquid is sent to the scum concentrating tank, and this mixed liquid and scum are again sucked by the scum skimmer. A scum removal method characterized by increasing the scum concentration in the mixed solution in the scum concentrating tank by repeating this and drawing out the mixed liquid having a high scum concentration in the scum concentrating tank. スカム濃縮槽からのスカム濃度の高い混合液を脱水処理することを特徴とする請求項1記載のスカムの除去方法。   The method for removing scum according to claim 1, wherein the mixed solution having a high scum concentration from the scum concentration tank is dehydrated. 水処理槽の水面付近に浮遊するスカムと活性汚泥とを含む混合液を吸入するスカムスキマーと、このスカムスキマーから吸入された混合液を圧送する圧送手段と、この圧送手段で圧送された混合液を一時的に貯留し、この混合液の一部を上記水処理槽に戻し、残部をスカムスキマーに吸入させるスカム濃縮槽を備えたことを特徴とするスカムの除去装置。   A scum skimmer for sucking a mixed liquid containing scum and activated sludge floating near the surface of the water treatment tank, a pressure feeding means for pumping the mixed liquid sucked from the scum skimmer, and a liquid mixture pumped by the pressure feeding means A scum removing device comprising a scum concentrating tank that temporarily stores a part of the mixed liquid, returns a part of the mixed liquid to the water treatment tank, and sucks the remaining part into a scum skimmer. スカム濃縮槽から混合液を引き抜き、この混合液を脱水処理する脱水処理装置をさらに備えた請求項3記載のスカムの除去装置。   4. The scum removing device according to claim 3, further comprising a dehydrating device for extracting the mixed solution from the scum concentrating tank and dehydrating the mixed solution. 請求項3または4記載のスカムの除去装置が水処理槽内に設置されていることを特徴とする廃水処理装置。
A wastewater treatment apparatus, wherein the scum removal device according to claim 3 or 4 is installed in a water treatment tank.
JP2004263883A 2004-09-10 2004-09-10 Scum removal method Withdrawn JP2006075765A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100997133B1 (en) 2010-03-26 2010-11-30 부경엔지니어링주식회사 Transfer speed control device of scum
JP2011112076A (en) * 2009-11-24 2011-06-09 Keihin Corp Solenoid valve device
FR3015465A1 (en) * 2013-12-24 2015-06-26 Sources SIMPLIFIED SYSTEM FOR SIMULTANEOUS EXTRACTION AND HOMOGENIZATION OF FLOATANTS AND SLUDGE OF WATER PURIFICATION STATIONS
CN105477909A (en) * 2015-12-15 2016-04-13 富凯迪沃(天津)环保科技有限公司 Upwards-floating sludge collector

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011112076A (en) * 2009-11-24 2011-06-09 Keihin Corp Solenoid valve device
KR100997133B1 (en) 2010-03-26 2010-11-30 부경엔지니어링주식회사 Transfer speed control device of scum
FR3015465A1 (en) * 2013-12-24 2015-06-26 Sources SIMPLIFIED SYSTEM FOR SIMULTANEOUS EXTRACTION AND HOMOGENIZATION OF FLOATANTS AND SLUDGE OF WATER PURIFICATION STATIONS
CN105477909A (en) * 2015-12-15 2016-04-13 富凯迪沃(天津)环保科技有限公司 Upwards-floating sludge collector

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