JP2515255B2 - Automatic adjustment device for sludge concentration in sewage treatment tank - Google Patents
Automatic adjustment device for sludge concentration in sewage treatment tankInfo
- Publication number
- JP2515255B2 JP2515255B2 JP62091513A JP9151387A JP2515255B2 JP 2515255 B2 JP2515255 B2 JP 2515255B2 JP 62091513 A JP62091513 A JP 62091513A JP 9151387 A JP9151387 A JP 9151387A JP 2515255 B2 JP2515255 B2 JP 2515255B2
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- treatment tank
- tank
- sludge concentration
- sewage treatment
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- 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.
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.
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.
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、曝気または撹拌によつて処理水の循環作用
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泥濃度調整
槽内へ導入された汚泥移送路と、汚泥濃度調整槽内の下
方部から導出されてその導出先端部を汚水処理槽内へ開
口させた汚泥還元路とに、夫々各別のポンプを附設する
かまたは電気バルブにより流路の切替がなされるように
して共通のポンプを附設し、汚泥濃度調整槽の上方部に
は該汚泥濃度調整槽内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
水処理槽内に透過型光センサーを装備して該光センサー
により、汚水処理槽内の汚泥濃度が所定濃度よりも高濃
度と判定されたときポンプによつて汚泥移送路が機能
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は上記汚泥移送路の機能が停止す
ると共にポンプによつて汚泥還元路が機能し得るよう電
気的に接続せられている。In the automatic sludge concentration adjusting device in the sewage treatment tank according to the present invention, the sewage treatment tank that circulates the treated water by aeration or agitation, and the sludge concentration that also performs aeration in addition to the precipitation action. A sludge transfer path having an adjusting tank and being led out from the lower part in the wastewater treatment tank and having its leading end portion introduced into the sludge concentration adjusting tank, and being led out from the lower part in the sludge concentration adjusting tank, A separate pump is attached to each of the sludge reduction channels with the discharge tip opening into the wastewater treatment tank, or a common pump is attached so that the flow path is switched by an electric valve, and the sludge concentration is increased. Provided in the upper part of the adjustment tank is a supernatant overflow channel for overflowing the supernatant water into the wastewater treatment tank when the water level in the sludge concentration adjustment tank rises, and a transmission type optical sensor is provided in the wastewater treatment tank. Then, by the optical sensor, sewage treatment tank If the sludge concentration in the wastewater treatment tank is determined to be higher than the predetermined concentration, the sludge transfer path will function by the pump, and if the sludge concentration in the wastewater treatment tank is determined to be lower than the predetermined concentration, the above sludge The function of the transfer path is stopped, and the sludge reduction path is electrically connected by the pump so that the function can be performed.
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は沈澱
槽型の汚泥濃度調整槽、2aは汚泥濃度調整槽2内に曝気
を施すための装置、3は汚水処理槽1内の下方部から高
濃度汚泥を汚泥濃度調整槽2内へ移送させるための汚泥
移送路、4は汚泥濃度調整槽1内の汚泥を汚水処理槽1
内へ還元させるための汚泥返送路であつて、第1図のよ
うに夫々各別のポンプPを附設するか、または第2図の
ように両者に共通のポンプPを附設して電気バルブ5に
より流路の切替がなされるよう構成する。6は汚泥濃度
調整槽2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2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。7は汚泥濃度調整槽2の下
方部から導出された排出路であつて、ポンプPにより余
剰汚泥を排出させる。8は汚水処理槽1内に装備せられ
た透過型光センサーであつて、該光センサー8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Pによつて汚泥移送機構3が機能し、
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Pによつて汚泥還元路4が機
能せしめられるよう電気的に接続しておくのである。9
は汚泥濃度調整槽2内の水位が低下した場合に後記水位
検知器10の検出信号により開作動する水道水供給バル
ブ、10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2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2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 aeration or stirring in the sewage treatment tank 1, 2 is a settling tank type sludge concentration adjusting tank, and 2a is aeration in the sludge concentration adjusting tank 2. 3 is a sludge transfer path for transferring high-concentration sludge from the lower part of the sludge treatment tank 1 into the sludge concentration adjusting tank 2, and 4 is a sludge treating tank for sludge in the sludge concentration adjusting tank 1. 1
The sludge return path for returning to the inside is provided with separate pumps P as shown in FIG. 1 or with a common pump P as shown in FIG. The flow path is switched by the above. Reference numeral 6 denotes a supernatant overflow channel that is led out from the upper part in the sludge concentration adjusting tank 2 and has its outlet opening end opened into the wastewater treatment tank 1. It has a role of overflowing into the sewage treatment tank 1. Reference numeral 7 denotes a discharge path led out from a lower part of the sludge concentration adjusting tank 2, and a pump P discharges excess sludge. Reference numeral 8 denotes a transmissive optical sensor installed in the sewage treatment tank 1. When the optical sensor 8 determines that the sludge concentration in the sewage treatment tank 1 is higher than a predetermined concentration, a pump P is used. The sludge transfer mechanism 3 works,
Further, when the sludge concentration in the sewage treatment tank 1 is determined to be lower than a predetermined concentration, the sludge reducing passage 4 is electrically connected by the pump P so as to function. 9
Is a tap water supply valve that opens when the water level in the sludge concentration adjusting tank 2 drops, and 10 is set to a level slightly lower than the constant water level in the sludge concentration adjusting tank 5. These are water level detectors, and after these settled sludge is returned from the lower part of the sludge concentration adjusting tank 2 into the sewage treatment tank 1, the water level in the sludge concentration adjusting tank 2 is restored to a constant water level for the next adjustment. This is to prepare for the 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によつて槽内液を循環させて均一な状
態となし、汚水処理槽1内に設定せられた透過型光セン
サー8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Pの駆動により汚泥移送路3が機
能して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2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2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2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6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 agitation device 1a circulates the liquid in the tank to make it a uniform state, and the sludge concentration is detected by the transmission type optical sensor 8 set in the wastewater treatment tank 1, and the concentration is higher than a predetermined value. If it is higher, the sludge transfer passage 3 functions by driving the pump P so that all or part of the circulating liquid flows into the sludge concentration adjusting tank 5. At that time, the sludge concentration adjusting tank 2 is set to perform intermittent or continuous aeration in synchronization with the wastewater treatment tank 1 except for the concentration adjusting time, and stop the aeration during the concentration adjusting time. As a result, the sludge concentration adjusting tank 2 is in a state of static sedimentation for about 1 to 3 hours, and during the sludge adjusting time, sludge particles in the sludge mixed solution transferred to the sludge treatment tank 1 are sludge. It precipitates in the lower part of the concentration adjusting tank 2, and the supernatant water overflows and flows back into the wastewater treatment tank 1 through the supernatant water overflow channel 6.
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2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8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。In this way, while the supernatant water from which sludge has been removed is recirculated, when high-concentration sludge is continuously transferred from the lower part of the wastewater treatment tank 1 into the sludge concentration adjusting tank 2, The sludge concentration gradually decreases and is diluted until it reaches a predetermined concentration detected by the transmissive optical sensor 8.
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8の検出信号によつて汚泥還元路4のポ
ンプPが働らき、汚泥濃度調整槽2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8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 P of the sludge reduction passage 4 is activated by the detection signal of the transmission type optical sensor 8 and settles down in the sludge concentration adjusting tank 2. The concentrated sludge is returned to the sewage treatment tank 1, and the transmission type optical sensor 8 continues until the sludge concentration in the sewage treatment tank 1 reaches a predetermined value.
上記汚泥の移送継続によつて汚泥濃度調整槽2内の水
位が低下した場合には、水位検知器10の検出信号により
水道水供給バルブ9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 2 decreases due to the continuous transfer of the sludge, the tap water supply valve 9 is opened by the detection signal of the water level detector 10 to supply water up to the constant water level. To prepare for the adjustment action.
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
ものであつて、第1図は汚泥移送路と汚泥還元路とに夫
々各別のポンプを附設した事例、第2図は汚泥移送路と
汚泥還元路とに共通のポンプを附設して電気バルブによ
り流路の切替がなされるようにした事例を示す。 1……汚水処理槽、2……汚泥濃度調整槽、3……汚泥
移送路、4……汚泥還元路、5……電気バルブ、6……
上澄水溢流路、8……透過型光センサー、P……ポン
プ。FIG. 1 is a vertical sectional view of an embodiment of the device of the present invention. FIG. 1 shows an example in which separate pumps are attached to the sludge transfer passage and the sludge return passage, and FIG. 2 shows sludge transfer. An example is shown in which a common pump is attached to the path and the sludge reduction path, and the flow path is switched by an electric valve. 1 ... sewage treatment tank, 2 ... sludge concentration adjusting tank, 3 ... sludge transfer path, 4 ... sludge reduction path, 5 ... electric valve, 6 ...
Clear water overflow channel, 8 ... Transmission type optical sensor, P ... Pump.
Claims (2)
を行わせる汚水処理槽(1)と沈澱作用を行わせる汚泥
濃度調整槽(2)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泥濃度調整槽
(2)内へ導入された汚泥移送路(3)と、汚泥濃度調
整槽(2)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)内へ開口させた汚泥還元路(4)と
に、夫々各別のポンプ(P)を附設するかまたは電気バ
ルブ(5)により流路の切替がなされるようにして共通
のポンプ(P)を附設し、汚泥濃度調整槽(2)の上方
部には該汚泥濃度調整槽(2)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
(6)を設け、かつ、汚水処理槽(1)内に透過型光セ
ンサー(8)を装備して該光センサー(8)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(P)によつて汚泥移送路(3)
が機能し、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は上記汚泥移送路
(3)の機能が停止すると共にポンプ(P)によつて汚
泥還元路(4)が機能し得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 a sewage treatment tank (1) for circulating treated water by aeration or agitation and a sludge concentration adjusting tank (2) for causing precipitation. Sludge transfer path (3) that is led out from the lower part of the sludge and has its leading end introduced into the sludge concentration adjusting tank (2), and the leading end that is led out from the lower part in the sludge concentration adjusting tank (2) A separate pump (P) is attached to each of the sludge reducing passages (4) whose parts are opened into the sewage treatment tank (1), or the flow paths are switched by an electric valve (5). And a common pump (P) is attached to the upper part of the sludge concentration adjusting tank (2), and when the water level in the sludge concentration adjusting tank (2) rises, the supernatant water overflows into the wastewater treatment tank (1). A clear water overflow channel (6) is provided, and a transmission type optical sensor (8) is installed in the wastewater treatment tank (1). The light sensor (8), sewage treatment tank (1) in by connexion sludge transfer path to the pump (P) when the sludge concentration is determined to a higher concentration than the predetermined concentration (3)
Function, and when the sludge concentration in the wastewater treatment tank (1) is determined to be lower than a predetermined concentration, the function of the sludge transfer path (3) is stopped and the sludge is pumped by the pump (P). An automatic adjustment device for sludge concentration in a sewage treatment tank, which is electrically connected so that the reduction path (4) can function.
を行わせる汚水処理槽(1)と曝気および沈澱作用を行
わせる汚泥濃度調整槽(2)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泥
濃度調整槽(2)内へ導入された汚泥移送路(3)と、
汚泥濃度調整槽(2)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)内へ開口させた汚泥還元路
(4)とに、夫々各別のポンプ(P)を附設するかまた
は電気バルブ(5)により流路の切替がなされるように
して共通のポンプ(P)を附設し、汚泥濃度調整槽
(2)の上方部には該汚泥濃度調整槽(2)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(6)を設け、かつ、汚水処理槽(1)内
に透過型光センサー(8)を装備して該光センサー
(8)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(P)によつて
汚泥移送路(3)が機能し、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は
上記汚泥移送路(3)の機能が停止すると共にポンプ
(P)によつて汚泥還元路(4)が機能し得るよう電気
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) having a sewage treatment tank (1) for circulating treated water by aeration or agitation and a sludge concentration adjusting tank (2) for performing aeration and precipitation. ), And a sludge transfer path (3) that is led out from the lower part of the inside of the above) and has its leading end portion introduced into the sludge concentration adjusting tank (2),
Separate pumps (P) are attached to the sludge reduction passage (4) that is led out from the lower part of the sludge concentration adjusting tank (2) and has its leading end opened into the wastewater treatment tank (1). Or a common pump (P) is attached so that the flow path is switched by the electric valve (5), and the sludge concentration adjusting tank (2) is provided above the sludge concentration adjusting tank (2). A clear water overflow channel (6) for overflowing the clear water into the sewage treatment tank (1) when the water level rises is provided, and a transmission type optical sensor (8) is provided in the sewage treatment tank (1). When the optical sensor (8) determines that the sludge concentration in the wastewater treatment tank (1) is higher than a predetermined concentration, the pump (P) causes the sludge transfer path (3) to function, and When it is determined that the sludge concentration in the wastewater treatment tank (1) is lower than a predetermined concentration, the sludge transfer path (3) is used. There becomes electrically connected to I connexion sludge reduction path to the pump (P) (4) can function to stop, automatic adjuster of the sludge concentration in the sewage treatment tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62091513A JP2515255B2 (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 |
---|---|---|---|
JP62091513A JP2515255B2 (en) | 1987-04-13 | 1987-04-13 | Automatic adjustment device for sludge concentration in sewage treatment tank |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS63256188A JPS63256188A (en) | 1988-10-24 |
JP2515255B2 true JP2515255B2 (en) | 1996-07-10 |
Family
ID=14028486
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62091513A Expired - Lifetime JP2515255B2 (en) | 1987-04-13 | 1987-04-13 | Automatic adjustment device for sludge concentration in sewage treatment tank |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2515255B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101645383B1 (en) * | 2015-10-06 | 2016-08-03 | 코오롱워터앤에너지 주식회사 | Apparatus for reducing sludge |
-
1987
- 1987-04-13 JP JP62091513A patent/JP2515255B2/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101645383B1 (en) * | 2015-10-06 | 2016-08-03 | 코오롱워터앤에너지 주식회사 | Apparatus for reducing sludge |
Also Published As
Publication number | Publication date |
---|---|
JPS63256188A (en) | 1988-10-24 |
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