JP2515256B2 - Automatic adjustment device for sludge concentration in sewage treatment tank - Google Patents

Automatic adjustment device for sludge concentration in sewage treatment tank

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Publication number
JP2515256B2
JP2515256B2 JP62091514A JP9151487A JP2515256B2 JP 2515256 B2 JP2515256 B2 JP 2515256B2 JP 62091514 A JP62091514 A JP 62091514A JP 9151487 A JP9151487 A JP 9151487A JP 2515256 B2 JP2515256 B2 JP 2515256B2
Authority
JP
Japan
Prior art keywords
sludge
treatment tank
sewage treatment
tank
pump
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 - Lifetime
Application number
JP62091514A
Other languages
Japanese (ja)
Other versions
JPS63256189A (en
Inventor
薫 三橋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TSURUMI SEISAKUSHO KK
Original Assignee
TSURUMI SEISAKUSHO KK
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Filing date
Publication date
Application filed by TSURUMI SEISAKUSHO KK filed Critical TSURUMI SEISAKUSHO KK
Priority to JP62091514A priority Critical patent/JP2515256B2/en
Publication of JPS63256189A publication Critical patent/JPS63256189A/en
Application granted granted Critical
Publication of JP2515256B2 publication Critical patent/JP2515256B2/en
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Expired - Lifetime 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

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  • Activated Sludge Processes (AREA)

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は、汚水処理槽内における汚泥濃度の自動調整
方法および装置に関するものである。
Description: TECHNICAL FIELD [0001] The present invention relates to a method and an apparatus for automatically adjusting sludge concentration in a sewage treatment tank.

〔発明の背景〕[Background of the Invention]

活性汚泥処理において処理の効率を高く保つために
は、処理すべき流入原水に対して働く一定の微生物量が
必要とされている。従来、活性汚泥法のような連続処理
では、処理槽への流入負荷が一定に保たれるよう予備貯
溜槽等を設け、また汚泥濃度が一定に保たれるよう定期
的に汚泥濃度を計測し、一定量比の汚泥を余剰汚泥とし
て系外に排出することが行われている。これには、JIS
に定められている懸濁物質の乾燥重量法等によつてMLSS
またはMLVSSを測定し、あるいは光電型濃度計を用いて
処理槽液の濃度を測定し、濃度が高いときは沈澱槽から
の汚泥の返送量を減少させ、余剰汚泥として排出する汚
泥の量比を増加させるのである。
In order to keep the treatment efficiency high in activated sludge treatment, a certain amount of microorganisms working on the inflow raw water to be treated is required. Conventionally, in continuous treatment such as the activated sludge method, a preliminary storage tank, etc. is provided to keep the inflow load into the treatment tank constant, and the sludge concentration is regularly measured to keep the sludge concentration constant. A certain amount of sludge is discharged as excess sludge out of the system. This includes JIS
MLSS using the dry weight method for suspended substances specified in
Alternatively, measure the MLVSS or measure the concentration of the treatment tank liquid using a photoelectric densitometer, and if the concentration is high, reduce the amount of sludge returned from the sedimentation tank, and change the sludge volume ratio discharged as excess sludge. Increase it.

しかし脱窒を目的とする活性汚泥法等においては、処
理槽内または硝化槽内に硝化菌を保持するため、汚泥の
引抜は慎重に行なわなければならない。特に汚泥の沈降
速度を曝気と非曝気の指標とする間欠曝気の自動運転法
(特許第1160241号)では、汚泥濃度を一定範囲内に保
つことが不可欠の要件となる。
However, in the activated sludge method for the purpose of denitrification, the sludge must be carefully extracted in order to keep the nitrifying bacteria in the treatment tank or the nitrification tank. Especially in the intermittent aeration automatic operation method (Patent No. 1160241) in which the sludge settling speed is used as an index of aeration and non-aeration, it is an essential requirement to keep the sludge concentration within a certain range.

〔発明の目的〕[Object of the Invention]

本発明の目的は、処理槽液中に常に一定の汚泥微生物
が保持せられ、余剰汚泥を少量にすると共に間欠曝気条
件に適合した汚泥濃度の調整を自動的に行わせることに
ある。
An object of the present invention is to constantly maintain a constant sludge microorganism in a treatment tank liquid, reduce the amount of excess sludge, and automatically adjust the sludge concentration suitable for intermittent aeration conditions.

〔発明の構成〕[Structure of Invention]

本発明に係る汚水処理槽内における汚泥濃度の自動調
整装置では、曝気または撹拌作用を行わせる汚水処理槽
と、沈澱作用のほか必要に応じ曝気をも行わせる汚泥濃
度調整槽とを有し、汚水処理槽内の下方部から導出され
てその導出先端部を汚水処理槽内の上方部へ開口させた
管路にポンプを附設して汚泥の循環回路となし、汚水処
理槽内の下方部から導出して汚泥調整槽内へ導入された
管路にポンプを附設することにより汚泥移送機構を構成
し、汚泥濃度調整槽の下方部より導出されてその導出先
端部汚水処理槽内の上方部へ開口させた管路にポンプを
附設することにより汚泥還元機構を構成し、汚泥濃度調
整槽の上方部には該汚泥濃度調整槽の水位上昇時におい
て上澄水を汚水処理槽内へ溢流させる上澄水溢流路を設
け、かつ、汚水処理槽内または汚泥の循環回路中に透過
型光センサーにより、汚水処理槽内の汚泥濃度が所定濃
度よりも高濃度と判定されるときポンプによつて汚泥移
送機構が作動し、また、汚水処理槽内の汚泥濃度が所定
濃度よりも低濃度と判定されたときポンプによつて汚泥
還元機構が作動せしめられるよう電気的に接続されてい
る。
The apparatus for automatically adjusting the sludge concentration in the sewage treatment tank according to the present invention has a sewage treatment tank for performing aeration or stirring, and a sludge concentration adjustment tank for performing aeration as well as a precipitation action, From the lower part of the sewage treatment tank, a pump is attached to the pipeline that is led out from the lower part of the sewage treatment tank and has its leading end opening to the upper part of the sewage treatment tank. A sludge transfer mechanism is constructed by attaching a pump to the pipeline that is led out and introduced into the sludge adjusting tank, and is led out from the lower part of the sludge concentration adjusting tank to the upper part inside the wastewater treatment tank. A sludge reduction mechanism is constructed by attaching a pump to the opened pipe, and the upper part of the sludge concentration adjusting tank is used to overflow the supernatant water into the wastewater treatment tank when the water level of the sludge concentration adjusting tank rises. A clear water overflow channel is provided and sewage treatment When the sludge concentration in the sewage treatment tank is judged to be higher than the specified concentration by the transmission type optical sensor inside or in the circulation circuit of the sludge, the sludge transfer mechanism is activated by the pump, and also in the sewage treatment tank. When the sludge concentration is determined to be lower than a predetermined concentration, the pump is electrically connected so that the sludge reducing mechanism is operated.

〔実施例〕〔Example〕

実施例の図面において、1は汚水処理槽、1aは汚水処
理槽1内に曝気または撹拌を施すための装置、2は汚水
処理槽1内の上方部へ開口させた管路3にポンプ4を装
備させてなる汚泥の循環回路、5は沈澱槽型の汚泥濃度
調整槽、5aは汚泥濃度調整槽5内に曝気を施すための装
置、6は汚泥調整槽1内の下方部から高濃度汚泥を汚泥
濃度調整槽5内へ移送させるための汚泥移送機構であつ
て、汚水処理槽1内の下方部から導出されて汚泥濃度調
整槽5内へ導入される管路3bにポンプ4bを附設すること
により構成される。8は汚泥濃度調整槽5内の上方部よ
り導出されてその導出開口端を汚水処理槽1内へ開口さ
せた上澄水溢流路で、汚泥濃度調整槽5内の水位上昇時
において上澄水を汚水処理槽1内へ溢流させる役割を有
する。9は汚泥濃度調整槽5内下方部の沈澱汚泥を汚水
処理槽1内へ還元させるための汚泥返還機構であつて、
汚泥濃度調整槽5内の下方部から導出されてその導出先
端部を汚水処理槽1内の上方部へ開口させた管路10にポ
ンプ11を装備して構成される。12は汚泥濃度調整槽5の
下方部から導出された排出路、13は排出路12によつて余
剰汚泥を汚泥濃度調整槽5の下方部から排出させるため
のポンプ、14は汚水処理槽1内または汚泥の循環回路中
に装備せられた透過型光センサーであつて、該光センサ
ー14により汚水処理槽1内の汚泥濃度が所定濃度よりも
高濃度と判定されたときポンプ4による汚泥移送機構6
が作動し、また、汚水処理槽1内の汚泥濃度が所定濃度
よりも低濃度と判定されたときポンプ11による汚泥還元
機構9が作動せしめられるよう電気的に接続しておくの
である。15は汚泥濃度調整槽5内の水位が低下した場合
に後記水位検知器16の検出信号により開作動する水道水
供給バルブ、16は汚泥濃度調整槽5内の定水位よりも若
干低い水位に設定せられた水位検知器で、これらは沈澱
汚泥が汚泥濃度調整槽5の下方部より汚水処理槽1内へ
還元されたのち、汚泥濃度調整槽5内の水位を定水位ま
で復元させて次の調整作用に備えるためのものである。
In the drawings of the embodiments, 1 is a sewage treatment tank, 1a is a device for aerating or stirring the sewage treatment tank 1, and 2 is a pump 4 in a pipe line 3 opened in the upper part of the sewage treatment tank 1. A sludge circulation circuit to be equipped, 5 is a sedimentation tank type sludge concentration adjusting tank, 5a is a device for aerating the sludge concentration adjusting tank 5, and 6 is a high concentration sludge from the lower part in the sludge adjusting tank 1. A sludge transfer mechanism for transferring the sludge to the sludge concentration adjusting tank 5, and a pump 4b is attached to the pipeline 3b which is led out from the lower part of the wastewater treatment tank 1 and introduced into the sludge concentration adjusting tank 5. It is composed of Reference numeral 8 is a supernatant water overflow channel which is led out from the upper part in the sludge concentration adjusting tank 5 and has its outlet opening end opened into the wastewater treatment tank 1, and clears the supernatant water when the water level in the sludge concentration adjusting tank 5 rises. It has a role of overflowing into the sewage treatment tank 1. Reference numeral 9 denotes a sludge return mechanism for reducing the settled sludge in the lower part of the sludge concentration adjusting tank 5 into the sewage treatment tank 1.
A pump 11 is provided in a pipe 10 which is led out from a lower part in the sludge concentration adjusting tank 5 and whose leading end is opened to an upper part in the sewage treatment tank 1. 12 is a discharge channel led out from the lower part of the sludge concentration adjusting tank 5, 13 is a pump for discharging excess sludge from the lower part of the sludge concentration adjusting tank 5 by the discharge channel 12, and 14 is the inside of the wastewater treatment tank 1. Alternatively, a transmission type optical sensor provided in the sludge circulation circuit, wherein when the optical sensor 14 determines that the sludge concentration in the wastewater treatment tank 1 is higher than a predetermined concentration, the sludge transfer mechanism by the pump 4 6
Is activated, and when the sludge concentration in the sewage treatment tank 1 is determined to be lower than a predetermined concentration, the sludge reduction mechanism 9 by the pump 11 is electrically connected so as to be activated. Reference numeral 15 is a tap water supply valve that opens when the water level in the sludge concentration adjusting tank 5 drops, and 16 is set to a level slightly lower than the constant water level in the sludge concentration adjusting tank 5. These are the water level detectors, and after these settled sludge is returned from the lower part of the sludge concentration adjusting tank 5 into the wastewater treatment tank 1, the water level in the sludge concentration adjusting tank 5 is restored to the constant water level and the next This is to prepare for the adjusting action.

汚水処理槽1内で間欠曝気を行つたのち汚泥の沈澱と
上澄水の放流を行わせ、再び間欠曝気処理に入つたとき
所定の低水位l0で濃度調整を行うが、その場合、曝気ま
たは撹拌の装置1aによつて槽内液を均一な状態となし、
ポンプ4の駆動により循環回路2を介して槽内液を循環
させ、汚水処理槽1内または循環回路2の途中に設定せ
られた透過型光センサー14によつて汚泥濃度を検出し、
その濃度が所定値よりも高い場合はポンプ4bを駆動させ
て汚泥移送機構6により循環液の全部または一部を汚泥
濃度調整槽5内へ流入させる。その際、汚泥濃度調整槽
5内には、濃度調整時間を除き汚水処理槽1内に同調し
た間欠または連続曝気を行い、濃度調整時間中は曝気を
停止するよう設定しておくのである。これによつて汚泥
濃度調整槽5内では沈澱放流時間約1〜3時間静止沈澱
の状態にあり、汚泥調整時間においては汚水処理槽1内
へ移送せられた汚泥混合液中の汚泥粒子は汚泥濃度調整
槽5内の下方部に沈澱し、上澄水が溢流となつて上澄水
溢流路8を通り汚水処理槽1内へ還流する。
After performing intermittent aeration in the sewage treatment tank 1, the sludge is precipitated and the supernatant water is discharged, and when the intermittent aeration process is performed again, the concentration is adjusted at a predetermined low water level l 0. The liquid in the tank is made uniform by the stirring device 1a,
The liquid in the tank is circulated through the circulation circuit 2 by driving the pump 4, and the sludge concentration is detected by the transmission type optical sensor 14 set in the sewage treatment tank 1 or in the middle of the circulation circuit 2,
When the concentration is higher than a predetermined value, the pump 4b is driven to cause the sludge transfer mechanism 6 to flow all or part of the circulating liquid into the sludge concentration adjusting tank 5. At this time, in the sludge concentration adjusting tank 5, intermittent or continuous aeration synchronized with the sewage treatment tank 1 is performed except for the concentration adjusting time, and the aeration is stopped during the concentration adjusting time. As a result, the sludge concentration adjusting tank 5 is in a stationary sedimentation time for about 1 to 3 hours, and during the sludge adjusting time, the sludge particles in the sludge mixture transferred into the sewage treatment tank 1 are sludge. The sedimentation occurs in the lower part of the concentration adjusting tank 5, and the supernatant water flows into the wastewater treatment tank 1 through the supernatant water overflow channel 8 as overflow.

このようにして汚泥の除去された上澄水が還流せられ
る一方で、汚水処理槽1内の下方部から高濃度の汚泥が
汚泥濃度調整槽5内へ移送し続けられると、汚水処理槽
1内の汚泥濃度は次第に低濃度となり、透過型光センサ
ー14で検出される所定濃度に達するまで稀釈されるので
ある。
While the supernatant water from which the sludge has been removed in this way is refluxed, while the high-concentration sludge is continuously transferred from the lower part of the sewage treatment tank 1 into the sludge concentration adjusting tank 5, the inside of the sewage treatment tank 1 The sludge concentration gradually becomes low, and is diluted until it reaches a predetermined concentration detected by the transmission type optical sensor 14.

また、汚水処理槽1内の汚泥量が減少したときは、透
過型光センサーの検出信号によつて汚泥還元機構9のポ
ンプ11が働らき、汚泥濃度調整槽5内の下方部に沈澱し
ている濃厚汚泥が汚水処理槽1内へ還元せられ、汚水処
理槽1内の汚泥濃度が所定値に達したことを透過型光セ
ンサー14によつて検出せられるまで継続される。
Further, when the amount of sludge in the sewage treatment tank 1 decreases, the pump 11 of the sludge reduction mechanism 9 operates according to the detection signal of the transmission type optical sensor, and sedimentation occurs in the lower part of the sludge concentration adjusting tank 5. The thick sludge is returned to the sewage treatment tank 1 and is continued until the transmission optical sensor 14 detects that the sludge concentration in the sewage treatment tank 1 has reached a predetermined value.

上記汚泥の移送継続によつて汚泥濃度調整槽5内の水
位が低下した場合には、水位検知器16の検出信号により
水道水供給バルブ15が開作動し、定水位まで水を供給し
て次の調整作用に備えるのである。
When the water level in the sludge concentration adjusting tank 5 is lowered due to the continuation of the sludge transfer, the tap water supply valve 15 is opened by the detection signal of the water level detector 16 to supply water to the constant water level and to supply water to the next water level. In preparation for the adjusting action of.

〔発明の効果〕〔The invention's effect〕

本発明によれば、汚水処理槽内における汚泥微生物の
増殖率が大きいときは汚泥を引抜いて汚泥濃度調整槽内
に貯溜し、自己消化によつて濃度が減少するときは汚泥
濃度調整槽より汚水処理槽へ汚泥を補充することによつ
て汚水処理槽内の汚泥濃度が調整せられ、汚水処理槽内
の液中に常に一定の汚泥微生物を保持せしめ得るという
利点がある。
According to the present invention, when the growth rate of sludge microorganisms in the sewage treatment tank is large, the sludge is drawn out and stored in the sludge concentration adjusting tank, and when the concentration decreases due to self-digestion, the sewage is discharged from the sludge concentration adjusting tank. By replenishing the sludge to the treatment tank, the sludge concentration in the wastewater treatment tank can be adjusted, and there is an advantage that a certain amount of sludge microorganisms can be always retained in the liquid in the wastewater treatment tank.

また、汚泥濃度調整槽内においては、引抜汚泥の他は
微生物の栄養源となる基質を加えずに間欠曝気を行つて
汚泥の量を減少せしめ、余剰汚泥量を少量にすると共に
間欠曝気条件に適合した汚泥微生物の活性化が体現され
る。これによつて汚水処理槽内へ補充するのに最も適し
た微生物を得ると共に、嫌気発酵によつてメタンガス等
を発生し、濃縮汚泥が膨化浮上するのを防ぐことができ
る。
In addition, in the sludge concentration adjustment tank, the amount of sludge is reduced by performing intermittent aeration without adding a substrate that is a nutrient source for microorganisms in addition to the extraction sludge, reducing the amount of excess sludge and intermittent aeration conditions. The activation of adapted sludge microorganisms is embodied. Thereby, microorganisms most suitable for replenishment into the sewage treatment tank can be obtained, and methane gas or the like can be generated by anaerobic fermentation to prevent the concentrated sludge from expanding and floating.

本発明方法および装置は、間欠曝気自動制御に必要と
されるばかりでなく、例えば小規模排水処理槽や、流入
負荷変動の大きい娯楽施設排水処理槽等においても果す
役割は大きく、また、活性汚泥法、オキシデーシヨンデ
イツチ、酸化池法等すべての生物懸濁態処理法に有用で
あり、装置の自動化、無人化および省エネルギー化に寄
与し得る等、産業上の利用性と有益性は多大である。
The method and apparatus of the present invention are not only required for automatic intermittent aeration control, but also play a large role in, for example, small-scale wastewater treatment tanks and recreational facility wastewater treatment tanks with large fluctuations in inflow load. The method is useful for all biological suspension treatment methods such as the oxidation method, oxidation date method, and oxidation pond method, and can contribute to automation, unmanned operation, and energy saving of equipment. It is.

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

図面は本発明装置の一実施例における縦断面図を示した
ものである。 1……汚水処理槽、2……循環回路、3……管路、3b…
…管路、4……ポンプ、4b……ポンプ、5……汚泥濃度
調整槽、6……汚泥移送機構、8……上澄水溢溜路、9
……汚泥還元機構、10……管路、11……ポンプ、14……
透過型光センサー。
The drawing shows a longitudinal sectional view of one embodiment of the device of the present invention. 1 ... sewage treatment tank, 2 ... circulation circuit, 3 ... pipe, 3b ...
... Pipe line, 4 ... Pump, 4b ... Pump, 5 ... Sludge concentration adjusting tank, 6 ... Sludge transfer mechanism, 8 ... Supernatant water overflow channel, 9
…… Sludge reduction mechanism, 10 …… Pipeline, 11 …… Pump, 14 ……
Transmissive optical sensor.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】曝気または撹拌作用の行われる汚水処理槽
(1)と沈澱作用の行われる汚泥濃度調整槽(5)とを
有し、汚水処理槽(1)内の下方部から導出されてその
導出先端部を汚水処理槽(1)内の上方部へ開口させた
管路(3)にポンプ(4)を附設して汚泥の循環回路
(2)となし、汚水処理槽(1)内の下方部から導出し
て汚泥調整槽(5)内へ導入された管路(3b)にポンプ
(4b)を附設することにより汚泥移送機構(6)を構成
し、汚泥温度調整槽(5)の下方部より導出されてその
導出先端部を汚水処理槽(1)内の上方部へ開口させた
管路(10)にポンプ(11)を附設することにより汚泥還
元機構(9)を構成し、汚泥濃度調整槽(5)の上方部
には該汚泥濃度調整槽(5)内の水位上昇時において上
澄水を汚水処理槽(1)内へ溢流させる上澄水溢流路
(8)を設け、かつ、汚水処理槽(1)内または汚泥の
循環回路(2)中に透過型光センサー(14)を装備して
該光センサー(14)により、汚水処理槽(1)内の汚泥
濃度が所定濃度よりも高濃度と判定されたときポンプ
(4)によつて汚泥移送機構(6)が作動し、また、汚
水処理槽(1)内の汚泥濃度が所定濃度よりも低濃度と
判定されたときポンプ(11)によつて汚泥還元機構
(9)が作動せしめられるよう電気的に接続してなる、
汚水処理槽内における汚泥濃度の自動調整装置。
1. A sewage treatment tank (1) having an aeration or stirring action and a sludge concentration adjusting tank (5) having a precipitation action, which is led out from a lower portion in the sewage treatment tank (1). Inside the sewage treatment tank (1), a pump (4) is attached to a pipe line (3) with its leading end opening to the upper part of the sewage treatment tank (1) to form a sludge circulation circuit (2). A sludge transfer mechanism (6) is constructed by attaching a pump (4b) to the pipeline (3b) that is led out from the lower part of the sludge and introduced into the sludge adjustment tank (5), and the sludge temperature adjustment tank (5) A sludge reduction mechanism (9) is constructed by attaching a pump (11) to a pipeline (10) that is led out from the lower part of the pipe and has its leading end opened to the upper part in the wastewater treatment tank (1). In the upper part of the sludge concentration adjusting tank (5), when the water level in the sludge concentration adjusting tank (5) rises, supernatant water is added to the wastewater treatment tank (1). A clear water overflow channel (8) for overflowing is provided, and a transmission type optical sensor (14) is provided in the wastewater treatment tank (1) or in the sludge circulation circuit (2) to provide the optical sensor ( When the sludge concentration in the sewage treatment tank (1) is determined to be higher than the predetermined concentration by 14), the sludge transfer mechanism (6) is operated by the pump (4), and the sewage treatment tank (1) When it is determined that the sludge concentration in) is lower than the predetermined concentration, the sludge reduction mechanism (9) is electrically connected by the pump (11).
Automatic adjustment device for sludge concentration in the sewage treatment tank.
【請求項2】曝気または撹拌作用の行われる汚水処理槽
(1)と曝気および沈澱作用の行われる汚泥濃度調整槽
(5)とを有し、汚水処理槽(1)内の下方部から導出
されてその導出先端部を汚水処理槽(1)内の上方部へ
開口させた管路(3)にポンプ(4)を附設して汚泥の
循環回路(2)となし、汚水処理槽(1)内の下方部か
ら導出して汚泥調整槽(5)内へ導入された管路(3b)
にポンプ(4b)を附設することにより汚泥移送機構
(6)を構成し、汚泥濃度調整槽(5)の下方部より導
出されてその導出先端部を汚水処理槽(1)内の上方部
へ開口させた管路(10)にポンプ(11)を附設すること
により汚泥還元機構(9)を構成し、汚泥濃度調整槽
(5)の上方部には該汚泥濃度調整槽(5)内の水位上
昇時において上澄水を汚水処理槽(1)内へ溢流させる
上溢水溢流路(8)を設け、かつ、汚水処理槽(1)内
または汚泥の循環回路(2)中に透過型光センサー(1
4)を装備して該光センサー(14)により、汚水処理槽
(1)内の汚泥濃度が所定濃度よりも高濃度と判定され
たときポンプ(4)によつて汚泥移送機構(6)が作動
し、また、汚水処理槽(1)内の汚泥濃度が所定濃度よ
りも低濃度と判定されたときポンプ(11)によつて汚泥
還元機構(9)が作動せしめられるよう電気的に接続し
てなる、汚水処理槽内における汚泥濃度の自動調整装
置。
2. A sewage treatment tank (1) which is aerated or stirred and a sludge concentration adjusting tank (5) which is aerated and settled, and is led from a lower part in the sewage treatment tank (1). Then, a pump (4) is attached to a pipeline (3) having an outlet end thereof opened upward in the wastewater treatment tank (1) to form a sludge circulation circuit (2). ) Pipe line (3b) led out from the lower part inside and introduced into the sludge adjusting tank (5)
A sludge transfer mechanism (6) is configured by attaching a pump (4b) to the sludge, and the sludge concentration adjusting tank (5) is led out from the lower portion and the leading end portion thereof is directed to the upper portion in the wastewater treatment tank (1). A sludge reduction mechanism (9) is configured by attaching a pump (11) to the opened pipeline (10), and the sludge concentration adjusting tank (5) is provided with an upper portion above the sludge concentration adjusting tank (5). An upper overflow channel (8) for overflowing the clear water into the sewage treatment tank (1) when the water level rises is provided, and a permeation type is provided in the sewage treatment tank (1) or the sludge circulation circuit (2). Light sensor (1
When the sludge concentration in the sewage treatment tank (1) is determined to be higher than a predetermined concentration by the optical sensor (14) equipped with the 4), the sludge transfer mechanism (6) is activated by the pump (4). When the sludge concentration in the sewage treatment tank (1) is determined to be lower than a predetermined concentration, it is electrically connected by a pump (11) so that the sludge reduction mechanism (9) is activated. Automatic adjustment device for sludge concentration in the sewage treatment tank.
JP62091514A 1987-04-13 1987-04-13 Automatic adjustment device for sludge concentration in sewage treatment tank Expired - Lifetime JP2515256B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62091514A JP2515256B2 (en) 1987-04-13 1987-04-13 Automatic adjustment device for sludge concentration in sewage treatment tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62091514A JP2515256B2 (en) 1987-04-13 1987-04-13 Automatic adjustment device for sludge concentration in sewage treatment tank

Publications (2)

Publication Number Publication Date
JPS63256189A JPS63256189A (en) 1988-10-24
JP2515256B2 true JP2515256B2 (en) 1996-07-10

Family

ID=14028514

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62091514A Expired - Lifetime JP2515256B2 (en) 1987-04-13 1987-04-13 Automatic adjustment device for sludge concentration in sewage treatment tank

Country Status (1)

Country Link
JP (1) JP2515256B2 (en)

Also Published As

Publication number Publication date
JPS63256189A (en) 1988-10-24

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