JP3455570B2 - Prevention method of soil accumulation in oxidation ditch - Google Patents

Prevention method of soil accumulation in oxidation ditch

Info

Publication number
JP3455570B2
JP3455570B2 JP28776093A JP28776093A JP3455570B2 JP 3455570 B2 JP3455570 B2 JP 3455570B2 JP 28776093 A JP28776093 A JP 28776093A JP 28776093 A JP28776093 A JP 28776093A JP 3455570 B2 JP3455570 B2 JP 3455570B2
Authority
JP
Japan
Prior art keywords
aerator
oxidation ditch
aerators
mechanical
sludge
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
JP28776093A
Other languages
Japanese (ja)
Other versions
JPH07116688A (en
Inventor
輝久 吉田
学 武内
Original Assignee
日立機電工業株式会社
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 日立機電工業株式会社 filed Critical 日立機電工業株式会社
Priority to JP28776093A priority Critical patent/JP3455570B2/en
Publication of JPH07116688A publication Critical patent/JPH07116688A/en
Application granted granted Critical
Publication of JP3455570B2 publication Critical patent/JP3455570B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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

Landscapes

  • Aeration Devices For Treatment Of Activated Polluted Sludge (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、オキシデーションディ
ッチの曝気槽において、汚砂が堆積腐敗するのを防止す
るために機械式曝気機の運転制御するようにしたオキシ
デーションディッチにおける汚砂の堆積防止方法に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an aeration tank of an oxidation ditch, in which the operation of a mechanical aerator is controlled so as to prevent the sediment from spoiling and spoiling. Regarding prevention methods.

【0002】[0002]

【従来の技術】近年、小規模下水道において、オキシデ
ーションディッチが各地で建設されているが、この方法
は曝気槽の前段に最初沈澱池を設けず、また面整備の初
期の段階では沈澱池も設けないため、曝気槽には汚砂が
直接に、しかも降雨時には多量に流入してくる。この汚
砂は無機の微細な砂を核として周囲に有機物が付着した
構造であるため、比重は無機砂より軽いが、曝気槽の活
性汚泥よりも重い1.05〜1.10程度であるため、
20cm/秒程度以上の流速を与えなければ沈降する。
2. Description of the Related Art In recent years, oxidation ditch has been constructed in various places in small-scale sewers, but this method does not first set a sedimentation tank before the aeration tank, and at the initial stage of surface maintenance Since it is not provided, dirty sand directly flows into the aeration tank, and a large amount of sand flows into it during rainfall. Since this filthy sand has a structure in which organic matter is attached to the surroundings with inorganic fine sand as the core, the specific gravity is lighter than inorganic sand, but is 1.05 to 1.10, which is heavier than activated sludge in the aeration tank. ,
If a flow rate of about 20 cm / sec or more is not applied, it will settle.

【0003】[0003]

【発明が解決しようとする課題】特にオキシデーション
ディッチの稼働後初期においては、流入する水量が少な
く、設置した曝気機の全台数を長時間運転すると過曝気
となって活性汚泥処理が解体することから、曝気機をフ
ル稼働できず、数台の曝気機のうちその一部を運転した
り、回転数を下げて低速運転しなければならず、そのた
め流速が低下して汚砂が堆積汚泥化し、この汚砂に付着
した有機物が腐敗するなどの問題がある。従って、流入
量に応じた曝気量に調整する必要がある。また処理場の
規模が小さいほど時間的な変動が大きいため、負荷変動
に応じて運転し、1日のうち流入量の多い時間帯には曝
気機をフル稼働させる場合があるが、堆積している汚砂
は活性汚泥よりも比重が大きいため、容易には巻き上げ
られず、堆積汚泥が腐敗する等の欠点がある。
In particular, in the initial period after the operation of the oxidation ditch, the amount of inflowing water is small, and if all the installed aerators are operated for a long time, they become over-aerated and the activated sludge treatment is dismantled. Therefore, the aerator cannot be fully operated and some of the several aerators must be operated, or the rotation speed must be reduced to operate at low speed, which reduces the flow velocity and turns the sludge into accumulated sludge. However, there is a problem that the organic matter attached to this dirty sand is decomposed. Therefore, it is necessary to adjust the aeration amount according to the inflow amount. Also, since the smaller the scale of the treatment plant is, the larger the temporal fluctuation is. Therefore, the aerator may be operated according to the load fluctuation, and the aerator may be fully operated during the time when the inflow is large in one day. Since the specific sludge has a larger specific gravity than the activated sludge, it cannot be easily rolled up and has the drawback that the accumulated sludge is decomposed.

【0004】本発明は、オキシデーションディッチ法の
曝気槽に汚砂が堆積して嫌気腐敗するのを防止するため
に、堆積を防止する方法を提供することを目的とする。
It is an object of the present invention to provide a method for preventing accumulation of dirty sand in an aeration tank of the oxidation ditch method so as to prevent anaerobic decay.

【0005】[0005]

【課題を解決するための手段】本発明は上記目的を達成
するためになしたもので、有機性排水を活性汚泥により
生物処理を行うオキシデーションディッチにおいて、曝
気槽の水面位置に機械式の曝気機を1台または複数台設
け、それらの曝気機の上流側の水槽底部に水中形の撹拌
機を設け、1日の間に少なくとも1回以上、機械式曝気
機を最高速運転または全台数運転する時間帯を設けて、
この時間帯に合わせて撹拌機を運転し、これにより汚砂
の堆積を防止することを要旨とする。
Means for Solving the Problems The present invention has been made to achieve the above object, and in an oxidation ditch in which organic wastewater is biologically treated with activated sludge, mechanical aeration is performed at a water surface position of an aeration tank. One or more machines are installed, and a submersible agitator is installed at the bottom of the water tank on the upstream side of those aerators, and the mechanical aerators are operated at the maximum speed or all units at least once a day. Set a time zone to
The gist is to operate the stirrer according to this time zone to prevent the accumulation of dirty sand.

【0006】[0006]

【作用】汚砂が堆積しやすい曝気機底部の上流側に水中
形の撹拌機を設け、曝気機を最高速運転または全台数運
転するフル稼働時に合わせて撹拌機を運転する。これに
より、堆積していた汚砂が巻き上げられるため、汚砂の
嫌気腐敗による活性汚泥の状態や処理水質の悪化を防止
することができる。
[Function] An underwater type agitator is provided on the upstream side of the bottom of the aerator where dirt is liable to accumulate, and the agitator is operated at the maximum operating speed of the aerators or at the time of full operation when all units are operated. As a result, the accumulated dirty sand is rolled up, so that it is possible to prevent the state of activated sludge and the deterioration of treated water quality due to anaerobic decay of the dirty sand.

【0007】[0007]

【実施例】以下、本発明オキシデーションディッチにお
ける汚砂の堆積防止方法の一実施例を図1乃至図3に基
づいて説明する。オキシデーションディッチの曝気槽1
は、図1に示すように所要の大きさ及び形状を有する。
例えば曝気槽1内に、図1に示すように所要の大きさの
長円形、または円形の循環水路を形成し、この曝気槽1
の水面に機械式の表面曝気機3を設ける。この表面曝気
機3の方式は図示のように、スクリュー形曝気機の他、
横軸ロータ状のもの、縦軸ロータ状のものが一般的に用
いられ、曝気槽の1槽に対し1台または2台以上の複数
台を適度に設けられる。さらにこの曝気槽1の底部に
は、曝気機3の上流側に水中形の撹拌機4を設置する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the method for preventing the accumulation of dirt in the oxidation ditch of the present invention will be described below with reference to FIGS. Oxidation Ditch aeration tank 1
Have the required size and shape as shown in FIG.
For example, as shown in FIG. 1, an oval or circular circulating water channel having a required size is formed in the aeration tank 1.
A mechanical surface aerator 3 is provided on the water surface. As shown in the figure, the system of this surface aerator 3 is, in addition to the screw type aerator,
A horizontal axis rotor type and a vertical axis rotor type are generally used, and one or a plurality of two or more aeration tanks are appropriately provided for each tank. Further, at the bottom of the aeration tank 1, an underwater agitator 4 is installed upstream of the aerator 3.

【0008】この設置台数は撹拌機4の能力や、曝気機
3の設置位置・台数を考慮して1台〜複数台設けるもの
とし、図1の実施例では長円形循環水路の直線部に夫々
曝気機と撹拌機とをセットとして配設する。また撹拌機
としてはプロペラ状の機械式撹拌機が一般的があるが、
必ずしもこれに限定されるものではなく、水中ポンプな
ど、別の撹拌手段を設けることも可能である。
Considering the capacity of the agitator 4 and the installation position / number of the aerators 3, the number of installed units is set to one to a plurality, and in the embodiment of FIG. An aerator and a stirrer are arranged as a set. As a stirrer, a propeller-shaped mechanical stirrer is generally used.
The present invention is not necessarily limited to this, and it is possible to provide another stirring means such as a submersible pump.

【0009】次に上述の如く構成した本発明のオキシデ
ーションディッチの動作・作用について説明する。曝気
機3の駆動によりその先端に設けたスクリュー31を回
転することにより、スクリュー先端部に負圧が発生する
が、スクリュー軸は中空状にしかも、水面上の中空シャ
フトにはスリットが設けられているため、このスリット
から空気が取り込まれ、スクリュー先端部に送られてス
クリューにより微細化されて水中に噴出される。またス
クリューの回転によって得られた撹拌水流によって活性
汚泥が浮遊すると共に、流入下水と活性汚泥が十分に混
合される。曝気機によって押し出された水流は、やがて
曝気槽のコーナー部に達し、コーナー壁面及びコーナー
ガイド2に沿って半周し、次の循環水路の直線部に配設
された曝気機に達して水路内に循環水流を形成する。
Next, the operation and action of the oxidation ditch of the present invention constructed as described above will be explained. By driving the aerator 3 to rotate the screw 31 provided at its tip, negative pressure is generated at the screw tip, but the screw shaft is hollow and the hollow shaft above the water surface is provided with slits. Therefore, air is taken in from this slit, sent to the tip of the screw, atomized by the screw, and jetted into the water. Further, the activated sludge floats due to the stirring water flow obtained by the rotation of the screw, and the inflow sewage and the activated sludge are sufficiently mixed. The water flow pushed out by the aerator eventually reaches the corner part of the aeration tank, makes a half turn along the corner wall surface and the corner guide 2, and reaches the aerator arranged in the straight part of the next circulation water channel and enters the water channel. Form a circulating water stream.

【0010】曝気機3の水深方向の流れは図2に示すよ
うに曝気機3から離れた位置では水面から底部まで整流
された流れになっているが、曝気直後の位置では噴出さ
れた微細な気泡aが斜め下方に向かって進み、やがて浮
上するため、このような気泡にともなう流れの影響でス
クリュー下部から下流にかけては槽底部付近で微少な渦
流が形成される。そのため流入した汚砂やシルトなど活
性汚泥よりも重い粒子が沈降しやすくなる。特に稼働開
始後初期の段階では、流入水量が少ないため、曝気機を
フル稼働することができず、曝気機の一部を運転した
り、間欠運転をしたり、あるいは回転数制御を行って曝
気量を減らすなどの特別な運転を行うことから、槽内の
循環流速はフル稼働時に比べて小さくなる。そのため汚
砂や汚砂に付着した汚泥分は最も流速が小さい曝気機の
下部に堆積する。
As shown in FIG. 2, the flow in the water depth direction of the aerator 3 is a flow rectified from the water surface to the bottom at a position distant from the aerator 3, but at the position immediately after the aeration, a fine jet of gas is ejected. Since the bubble a advances obliquely downward and floats up, a minute vortex is formed near the bottom of the tank from the lower part of the screw to the downstream due to the effect of the flow accompanying the bubble. Therefore, particles that are heavier than activated sludge such as inflowing sand and silt are likely to settle. Especially in the early stage after the start of operation, the aeration machine cannot be fully operated due to the small amount of inflowing water, and a part of the aeration machine is operated, intermittent operation is performed, or rotation speed control is performed to perform aeration. Due to special operation such as reducing the amount, the circulation flow velocity in the tank becomes smaller than that at full operation. Therefore, the sludge and the sludge adhering to the sludge are accumulated in the lower part of the aerator where the flow velocity is the lowest.

【0011】水路内では最も流速が小さい曝気機の下部
に堆積する汚泥を、本発明では1日の間に少なくとも1
回は曝気機をフル稼働する時間帯を設けて平均流速を高
め、さらに汚砂などの重い堆積物を巻き上げるための曝
気機の上流側底部に設けた撹拌機4のスクリュー41を
回転して撹拌機による水流を堆積物に直接作用させるよ
うになす。
In the present invention, at least 1 sludge is accumulated in the lower part of the aerator having the smallest flow velocity in the water channel in the present invention.
This time, the screw 41 of the stirrer 4 provided on the upstream bottom of the aerator for rotating the aerator to increase the average flow velocity to increase the average flow velocity and to wind up heavy sediment such as dirty sand is rotated and stirred. The machine water flow is applied directly to the sediment.

【0012】このような運転スケジュールの一例を図3
に示す。流入水量の多い時間帯に合わせて曝気機の全台
数を同時に運転すると共に、オーバーフローして沈澱池
に導かれ、沈澱した汚砂の一部は汚泥と共に余剰汚泥と
して排出される。また撹拌機を停止すると、底部流速は
徐々に低下してくるため、浮遊していた汚砂は流速の最
も遅い部分、すなわち曝気機の下部に堆積し始める。従
って1日の大半の時間帯は汚砂は堆積した状態となる
が、1日に1回は曝気機の全台数を同時に運転されるの
で、槽底部に沈澱した汚泥は巻き上げられ、水中に浮遊
して、溶存酸素の供給を受けるため、汚砂に付着した汚
泥等の有機物が嫌気腐敗するのを防止することができ
る。
An example of such an operation schedule is shown in FIG.
Shown in. All of the aerators are operated at the same time according to the time when the amount of inflowing water is large, and they are overflowed and guided to the settling basin, and part of the settled sludge is discharged together with the sludge as excess sludge. Further, when the stirrer is stopped, the bottom flow velocity gradually decreases, so the suspended sediment begins to accumulate at the slowest flow velocity part, that is, at the bottom of the aerator. Therefore, most of the time of the day, the sludge will be accumulated, but once a day, all the aerators are operated at the same time, so the sludge settled at the bottom of the tank is rolled up and floated in the water. Then, since the dissolved oxygen is supplied, it is possible to prevent anaerobic decay of organic matter such as sludge attached to the dirty sand.

【0013】なお、実施例ではスクリュー形曝気機の場
合を示したが、横軸ロータや縦軸ロータの場合も同様に
底部流速が最も小さくなるのが曝気機の下部及びその近
接する領域であるため、曝気機の上流側底部に撹拌機を
設けて本発明の運転を行うことにより、同様の作用・効
果を得ることができる。
In the embodiment, the case of the screw type aerator has been shown, but similarly in the case of the horizontal axis rotor and the vertical axis rotor, the bottom flow velocity is also the lowest in the lower part of the aerator and its adjacent region. Therefore, by providing the stirrer on the upstream side bottom of the aerator and performing the operation of the present invention, the same action and effect can be obtained.

【0014】[0014]

【発明の効果】本発明オキシデーションディッチにおけ
る汚砂の堆積防止方法は、曝気槽の水面位置に機械式の
曝気機を1台または複数台設け、それらの曝気機の上流
側の水槽底部に水中形の撹拌機を設け、1日の間に少な
くとも1回以上、機械式曝気機を最高速運転または全台
数運転する時間帯を設けて、この時間帯に合わせて撹拌
機を運転するようにしているため、汚砂と共に沈降した
有機物の腐敗及びそれに伴う水処理の悪化を防止でき、
また曝気機のフル稼働時において不足する流速を補うだ
けの撹拌機を最も適切な位置に配置するので、撹拌機の
設備動力を小さくでき、さらに撹拌機は曝気機のフル稼
働時に合わせて、最小限の運転を行うため、エネルギー
消費が少なくすることができる等の利点を有する。
The method for preventing the accumulation of dirt in the oxidation ditch of the present invention provides one or a plurality of mechanical aerators at the water surface position of the aeration tank, and the water tank at the bottom of the water tank upstream of these aerators. -Type stirrer is provided, and a time zone for operating the mechanical aerators at the highest speed or for all units is provided at least once a day. Therefore, it is possible to prevent the decomposition of the organic matter that has settled together with the dirty sand and the deterioration of water treatment accompanying it,
In addition, since the agitator, which only compensates for the insufficient flow rate when the aerator is fully operating, is placed at the most appropriate position, the equipment power of the agitator can be reduced, and the agitator can be set to the minimum when the aerator is fully operating Since the operation is limited, the energy consumption can be reduced.

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

【図1】本発明オキシデーションディッチにおける汚砂
の堆積防止方法の一実施例を示す平面図である。
FIG. 1 is a plan view showing an embodiment of a method for preventing dirt accumulation in an oxidation ditch according to the present invention.

【図2】同縦断面図である。FIG. 2 is a vertical sectional view of the same.

【図3】本発明による運転のタイムスケジュール図であ
る。
FIG. 3 is a time schedule diagram of an operation according to the present invention.

【符号の説明】[Explanation of symbols]

1 曝気槽 2 コーナーガイド 3 スクリュー形曝気機 4 撹拌機 a 気泡 b 堆積物 1 aeration tank 2 corner guide 3 screw type aerator 4 stirrer a bubble b sediment

フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C02F 3/14 - 3/26 Continuation of front page (58) Fields surveyed (Int.Cl. 7 , DB name) C02F 3/14-3/26

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 有機性排水を活性汚泥により生物処理を
行うオキシデーションディッチにおいて、曝気槽の水面
位置に機械式の曝気機を1台または複数台設け、それら
の曝気機の上流側の水槽底部に水中形の撹拌機を設け、
1日の間に少なくとも1回以上、機械式曝気機を最高速
運転または全台数運転する時間帯を設けて、この時間帯
に合わせて撹拌機を運転し、これにより汚砂の堆積を防
止することを特徴とするオキシデーションディッチにお
ける汚砂の堆積防止方法。
1. In an oxidation ditch for biological treatment of organic wastewater with activated sludge, one or more mechanical aerators are provided at the water surface of the aeration tank, and the bottom of the aquarium upstream of these aerators is provided. An underwater stirrer is installed in
Provide a time zone for operating the mechanical aerator at the highest speed or all units at least once during the day, and operate the agitator in accordance with this time zone to prevent the accumulation of dirt. A method for preventing accumulation of foul sand in an oxidation ditch, which is characterized in that
【請求項2】 機械式曝気機がスクリュー式であること
を特徴とする請求項1記載のオキシデーションディッチ
における汚砂の堆積防止方法。
2. The method for preventing accumulation of dirty sand in an oxidation ditch according to claim 1, wherein the mechanical aerator is a screw type.
【請求項3】 機械式曝気機が横軸または縦軸ロータ状
の表面曝気機であることを特徴とする請求項1記載の
キシデーションディッチにおける汚砂の堆積防止方法。
3. The method for preventing accumulation of dirt in an oxidation ditch according to claim 1, wherein the mechanical aerator is a surface aerator having a horizontal axis or a vertical axis rotor.
JP28776093A 1993-10-22 1993-10-22 Prevention method of soil accumulation in oxidation ditch Expired - Fee Related JP3455570B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28776093A JP3455570B2 (en) 1993-10-22 1993-10-22 Prevention method of soil accumulation in oxidation ditch

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28776093A JP3455570B2 (en) 1993-10-22 1993-10-22 Prevention method of soil accumulation in oxidation ditch

Publications (2)

Publication Number Publication Date
JPH07116688A JPH07116688A (en) 1995-05-09
JP3455570B2 true JP3455570B2 (en) 2003-10-14

Family

ID=17721405

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28776093A Expired - Fee Related JP3455570B2 (en) 1993-10-22 1993-10-22 Prevention method of soil accumulation in oxidation ditch

Country Status (1)

Country Link
JP (1) JP3455570B2 (en)

Also Published As

Publication number Publication date
JPH07116688A (en) 1995-05-09

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