JPS60206491A - Apparatus for treatment of waste water - Google Patents

Apparatus for treatment of waste water

Info

Publication number
JPS60206491A
JPS60206491A JP59061883A JP6188384A JPS60206491A JP S60206491 A JPS60206491 A JP S60206491A JP 59061883 A JP59061883 A JP 59061883A JP 6188384 A JP6188384 A JP 6188384A JP S60206491 A JPS60206491 A JP S60206491A
Authority
JP
Japan
Prior art keywords
tank
amount
sent
waste water
control apparatus
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.)
Pending
Application number
JP59061883A
Other languages
Japanese (ja)
Inventor
Chiaki Niwa
千明 丹羽
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.)
Shimizu Construction Co Ltd
Original Assignee
Shimizu Construction Co Ltd
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 Shimizu Construction Co Ltd filed Critical Shimizu Construction Co Ltd
Priority to JP59061883A priority Critical patent/JPS60206491A/en
Publication of JPS60206491A publication Critical patent/JPS60206491A/en
Pending 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

  • Activated Sludge Processes (AREA)

Abstract

PURPOSE:To miniaturize a water quality control apparatus and to obtain stable treated water quality, by mounting a flow amount control apparatus of raw waste water, a waste water retraction tank for retracting waste water exceeding a controlled amount, a water quality measuring instrument of treated water and the control apparatus of the flow amount control apparatus. CONSTITUTION:Raw waste apparatus is sent to flow amount control apparatus 11 where a predetermined amount of waste water controlled by a control apparatus 22 is sent to an aeration tank 12. When the amount of inflow raw waste water exceeds the control amount of raw waste water sent to the aeration tank 12, the excessive raw waste water is sent to a retraction tank 13 and temporarily stored therein. The raw waste water sent to the aeration tank 12 receives biological treatment according to a usual method and treated water is sent to a precipitation tank 17 to separate activated sludge while supernatant treated water is discharged to the outside through a monitor tank 20. The variation in the inflow amount of waste water is controlled by the flow amount control apparatus 11 and the amount of waste water sent to the aeration tank 12 is determined so as to always obtain good quality treated water.

Description

【発明の詳細な説明】 本発明は、廃水処理装置に関する。[Detailed description of the invention] The present invention relates to a wastewater treatment device.

第1図は、従来の一般的な廃水処理装置を示すものであ
る。この廃水処理装置によって有機性廃水を処理するに
は、まず原廃水を流量調整槽1に送る。流量調整槽1に
一旦貯留された原廃水は、その一定量がポンプ2で曝気
槽3に送液され、ここでブロア4からの空気が散気管5
から曝気WI3内に散気され、槽3内の活性汚泥によっ
て生物処理される。生物処理された廃水はついで曝、気
槽3から抜液され、沈澱槽6に送られる。沈澱槽6では
汚泥が沈澱し、上澄みの処理水が外部に放流されるとと
もに沈澱汚泥が曝気槽3に返送され、ここでの曝気処理
に供されるようになっている。
FIG. 1 shows a conventional general wastewater treatment device. In order to treat organic wastewater with this wastewater treatment device, raw wastewater is first sent to the flow rate adjustment tank 1 . A fixed amount of the raw wastewater once stored in the flow rate adjustment tank 1 is sent to the aeration tank 3 by the pump 2, where air from the blower 4 is passed through the aeration pipe 5.
Aeration is diffused into the aeration WI3, and the activated sludge in the tank 3 is used for biological treatment. The biologically treated wastewater is then aerated, drained from the aeration tank 3, and sent to a settling tank 6. The sludge is settled in the settling tank 6, and the supernatant treated water is discharged to the outside, and the settled sludge is returned to the aeration tank 3, where it is subjected to aeration treatment.

ところで、排出源から排出される原廃水の流量、水質は
時間的に大幅に変動するのが一般的である。
Incidentally, the flow rate and water quality of raw wastewater discharged from a discharge source generally vary significantly over time.

このため、第1図の従来の処理装置にあっては、上記流
量調整槽1を設置し、ここに原廃水を一時的に貯留し、
後段の曝気槽3へ常時基準値を満足する処理水が得られ
るように一定量の原廃水を送液するようにしている。
For this reason, in the conventional treatment equipment shown in FIG. 1, the flow rate adjustment tank 1 is installed, and raw wastewater is temporarily stored there.
A fixed amount of raw wastewater is sent to the subsequent aeration tank 3 so that treated water that always satisfies the standard value is obtained.

しかしながら、廃水処理装置の処理能力は流入原廃水の
水質の最大負荷に対応できるように設置され、よって装
置全体として平均すると能力的に過剰となっている。特
に、流量調整槽1は、曝気槽3以降の処理系統を小型化
しても、流入原廃水量の変動、を平均化するという上記
目的を達するためにどうしても大型となり、処理装置全
体の半分以上を占めることが応々にあり、設備費が嵩む
大きな原因となっていた。
However, the processing capacity of the wastewater treatment equipment is installed so as to be able to handle the maximum load of the water quality of the inflow source wastewater, and therefore, on average, the equipment as a whole has excess capacity. In particular, even if the treatment system after the aeration tank 3 is downsized, the flow rate adjustment tank 1 inevitably becomes large in order to achieve the above objective of equalizing fluctuations in the amount of inflow raw wastewater, and it takes up more than half of the entire treatment equipment. This was a major cause of increased equipment costs.

この発明は上記事情に鑑みてなされたもので、流量原廃
水の流量、水質を調整するだめの槽を極めて小形化でき
、しかも常に安定した処理水質を得ることができる廃水
処理装置を提供することを目的とするものである。
This invention has been made in view of the above circumstances, and an object of the present invention is to provide a wastewater treatment device that can extremely downsize a tank for adjusting the flow rate and water quality of raw wastewater, and can always obtain stable treated water quality. The purpose is to

以下、図面を参照してこの発明の詳細な説明する。Hereinafter, the present invention will be described in detail with reference to the drawings.

第2図は、本発明の廃水処理装置の一例を示すもので、
有機性廃水の活性汚泥処理に適用したものである。
FIG. 2 shows an example of the wastewater treatment device of the present invention.
This is applied to activated sludge treatment of organic wastewater.

図中符号11は、流量調節装置である。この流量調節装
置11は、後段の曝気槽12へ送液する原廃水量を所定
量に調節するもので、例えば小型の計量槽とこの計量槽
からの流量を調節する電動弁とからなるものや、可動堰
を設けた小型水槽などが用いられる。この流量調節装置
11で流量調節され、過剰となった原廃水は退避槽13
に送られ、ここで一時貯留される。退避槽13は小容量
の貯留槽であって、槽13内にはここに貯留された原廃
水を上記流量調節装置11または曝気槽12に送るポン
プ14が設けられている。曝気槽12は、ブロア15か
らの空気を槽12内に散気する散気管16を設け、活性
汚泥によって流入する原廃水を生物処理する通常のもの
である。また、符号17は沈澱槽である。この沈澱槽1
7も一般的なものであって、槽17底部には沈澱汚泥を
抜く抜液パイプ18が設けられている。そして、上記曝
気槽12と沈澱槽17とでこの例の処理装置本体が構成
される。但し、曝気槽12、沈澱槽17が一体化してい
るもの等特種なものでもかまわない。また、沈澱槽17
には沈降汚泥の界面を常時監視する汚泥界面計19が設
けられている。さらに、この沈澱槽17の後段には監視
槽20が設を 置されている。この監視槽20には、ここに流入する処
理水の水質を計測する水質計測器21、例えばTOC計
、COD計、Uv計、l) H計などが1種以上設けら
れている。また、制御量N22が設けられている。この
制御装置22は、汚泥界面H]19および水質計測器2
1からの信号を入力し、この入力信号に基づいて流量調
節装置11を制御して曝気WJ12への原廃水の送液m
を調節し、また退避槽13のポンプ14の動作を制御し
て退避槽13内の原廃水を所定量流量調節装置11ある
いは曝気槽12に送液せしめるものである。
Reference numeral 11 in the figure is a flow rate adjustment device. This flow rate adjustment device 11 adjusts the amount of raw wastewater sent to the subsequent aeration tank 12 to a predetermined amount, and for example, it may consist of a small metering tank and an electric valve that adjusts the flow rate from this metering tank. , a small aquarium with a movable weir is used. The flow rate is adjusted by this flow rate adjustment device 11, and the excess raw wastewater is removed from the evacuation tank 13.
and is temporarily stored there. The evacuation tank 13 is a small-capacity storage tank, and a pump 14 is provided in the tank 13 to send the raw wastewater stored here to the flow rate adjustment device 11 or the aeration tank 12. The aeration tank 12 is a conventional aeration tank that is provided with an aeration pipe 16 that diffuses air from a blower 15 into the tank 12, and that uses activated sludge to biologically treat incoming raw wastewater. Moreover, the code|symbol 17 is a settling tank. This settling tank 1
7 is also a common type, and a drainage pipe 18 is provided at the bottom of the tank 17 to remove the settled sludge. The aeration tank 12 and settling tank 17 constitute the main body of the processing apparatus in this example. However, a special type such as one in which the aeration tank 12 and the settling tank 17 are integrated may also be used. In addition, settling tank 17
is equipped with a sludge interface meter 19 that constantly monitors the interface of settled sludge. Further, a monitoring tank 20 is installed downstream of the settling tank 17. The monitoring tank 20 is provided with one or more types of water quality measuring devices 21 for measuring the quality of the treated water flowing therein, such as a TOC meter, a COD meter, a Uv meter, and an H meter. Further, a control amount N22 is provided. This control device 22 includes a sludge interface H] 19 and a water quality measuring device 2.
1 and controls the flow rate regulator 11 based on this input signal to send raw wastewater to the aeration WJ 12.
It also controls the operation of the pump 14 of the evacuation tank 13 to send a predetermined amount of raw wastewater in the evacuation tank 13 to the flow rate adjustment device 11 or the aeration tank 12.

つぎに、上記廃水処理装置の運転方法および作用を説明
する。
Next, the operating method and operation of the wastewater treatment apparatus will be explained.

原廃水はまず流量調節装置11に送られ、ここで制御装
置22によって制御された所定量の原廃水がただちに曝
気槽12に送られる。そして、流入原廃水量が曝気槽1
2に送られる原廃水の制御量を超えたときは、その余剰
原廃水が退避槽13に送られ、一時貯留される。曝気槽
12に送られた原廃水は、常法によって生物処理され、
処理水は沈澱槽17に送られて活性汚泥が分離され、上
澄処理水が監視槽20を経て、外部に排出される。
The raw wastewater is first sent to the flow rate regulating device 11, where a predetermined amount of raw wastewater controlled by the control device 22 is immediately sent to the aeration tank 12. Then, the inflow source wastewater amount is
When the amount of raw wastewater sent to tank 2 exceeds the control amount, the surplus raw wastewater is sent to the evacuation tank 13 and temporarily stored. The raw wastewater sent to the aeration tank 12 is biologically treated by a conventional method,
The treated water is sent to a settling tank 17, where activated sludge is separated, and the supernatant treated water is discharged to the outside via a monitoring tank 20.

この運転中、曝気槽12への原廃水の送液量が多すぎる
と、沈澱槽17での汚泥界面が上昇し、ここでの固液分
離が不可能となる。そこで、汚泥界面が所定よりも上昇
したならば、これを汚泥界面計19が検知し、この信号
が制御装置22に送られる。制御装置22はこの信号に
基づいて流量調節装fi111を制御し、原廃水の曝気
槽12への送液量を減少させ、汚泥界面を一定に保つよ
うにする。流量調節装置11で曝気槽12への送液量を
減少させることにより、余剰となった原廃水は退避槽1
3に送られる。また、汚泥界面が所定よりも低下すると
、制御装置22が同様に功き曝気槽12への送液量を増
加させる。この時、この送液量が原廃水の流入量を上回
った時は、退避槽13のポンプ14を動作させて、退避
槽13内に貯留された原廃水を流量調節装置11あるい
は曝気槽12に送給し、所定量の原廃水が曝気槽12に
送られるようにする。
During this operation, if the amount of raw wastewater sent to the aeration tank 12 is too large, the sludge interface in the settling tank 17 will rise, making solid-liquid separation impossible here. Therefore, if the sludge interface rises above a predetermined level, the sludge interface meter 19 detects this and sends this signal to the control device 22. The control device 22 controls the flow rate adjustment device fi111 based on this signal to reduce the amount of raw wastewater sent to the aeration tank 12 and keep the sludge interface constant. By reducing the amount of liquid sent to the aeration tank 12 with the flow rate adjustment device 11, excess raw wastewater is transferred to the evacuation tank 1.
Sent to 3. Further, when the sludge interface becomes lower than a predetermined value, the control device 22 similarly operates to increase the amount of liquid sent to the aeration tank 12. At this time, when the amount of liquid sent exceeds the inflow amount of raw wastewater, the pump 14 of the evacuation tank 13 is operated to transfer the raw wastewater stored in the evacuation tank 13 to the flow rate adjustment device 11 or the aeration tank 12. A predetermined amount of raw wastewater is sent to the aeration tank 12.

同時に、監視槽20の水質計測器21で計測された処理
水質が低下し、基準値以上となった場合には、制御装置
22は、この信号に基づいて流ム1調節装置11を制御
し、曝気槽12への原廃水の送液量を減少させ、曝気槽
12での原廃水の滞留時間を長くし、基準値以下の水質
の処理水が得られるようにする。余った原廃水は先と同
様に退避槽13に送られ、一時貯留される。また、処理
水質が基準値を下回って処理負荷に余裕が生じた場合に
は、退避槽13のポンプ14を動作させて退避槽13内
に貯留された原廃水を流量調節装置11あるいは曝気槽
12に送液する。
At the same time, if the treated water quality measured by the water quality measuring device 21 of the monitoring tank 20 decreases and becomes equal to or higher than the reference value, the control device 22 controls the flow 1 adjustment device 11 based on this signal, The amount of raw wastewater sent to the aeration tank 12 is reduced, the residence time of the raw wastewater in the aeration tank 12 is increased, and treated water of water quality below a standard value is obtained. The remaining raw wastewater is sent to the evacuation tank 13 and temporarily stored in the same manner as before. In addition, when the treated water quality is below the standard value and there is a surplus in the treatment load, the pump 14 of the evacuation tank 13 is operated to transfer the raw wastewater stored in the evacuation tank 13 to the flow rate adjustment device 11 or the aeration tank 12. Send liquid to.

このように、この例の装置にあっては、曝気槽12への
原廃水の送液量を、この送液量と処理水質との両面から
同時に制御している。ただし、この例では基準値以下の
処理水質が得られぬのは、原廃水の送液容量だけが原因
ではなく、例えば原廃水の汚れの度合なども関係するの
で、汚泥界面計19の信号で制御される送液量にはりミ
ツターをかけて、最低限の原廃水を曝気槽12へ供給す
るようにする必要がある。
In this way, in the apparatus of this example, the amount of raw wastewater sent to the aeration tank 12 is simultaneously controlled from the viewpoint of both the amount of liquid sent and the quality of the treated water. However, in this example, the reason why the treated water quality is not below the standard value is not only due to the feeding capacity of the raw wastewater, but is also related to, for example, the degree of contamination of the raw wastewater, so the signal from the sludge interface meter 19 It is necessary to set a limit on the amount of liquid to be controlled so that the minimum amount of raw wastewater is supplied to the aeration tank 12.

このような処理装置にあっては、流入廃水量の変動を流
量調節装置11で制御し、常に良好な処理水質が得られ
るように曝気槽12への送液量を定め、余剰の原廃水の
みを退避槽13に送ることができるので、退避槽13に
一時貯留される原廃水量は少なくなり、退避槽13は十
分小容量のものでよく、設備費用の低減を図ることがで
きる。
In such a treatment device, fluctuations in the amount of inflowing wastewater are controlled by a flow rate regulator 11, the amount of liquid sent to the aeration tank 12 is determined so that good treated water quality is always obtained, and only excess raw wastewater is can be sent to the evacuation tank 13, the amount of raw wastewater temporarily stored in the evacuation tank 13 is reduced, and the evacuation tank 13 only needs to have a sufficiently small capacity, which can reduce equipment costs.

また、処理水質によって曝気槽12への送液量を調節す
ることができるので、処理水の水質も安定するとともに
放流水質の監視をも同時に行える。
Furthermore, since the amount of liquid sent to the aeration tank 12 can be adjusted depending on the quality of the treated water, the quality of the treated water is stabilized and the quality of the discharged water can be monitored at the same time.

なお、本発明は上記実施例に限定されるものではなく、
原廃水が例えば含窒素有機性廃水の場合には、処理装置
本体として沈澱槽17の後段に硝化槽、脱窒槽を追加設
置したものが用いられ、処理対象廃水の種類、処理装置
本体の種類のいかんにかかわらず、流量調節装置11、
退避1113 。
Note that the present invention is not limited to the above embodiments,
If the raw wastewater is, for example, nitrogen-containing organic wastewater, the main body of the treatment equipment used is a nitrification tank and a denitrification tank installed after the settling tank 17, and the type of wastewater to be treated and the type of the main body of the treatment equipment are Regardless of the flow rate adjustment device 11,
Evacuation 1113.

水質計測器21および制御装置22を備えておれば、同
様の作用効果が得られる。
If the water quality meter 21 and the control device 22 are provided, similar effects can be obtained.

以上説明したように、本発明の廃水処理装置は、原廃水
の廃水処理装置本体への送液量を所定量に 瞥調節する
流量調節装置と、この流量調節装置による調WI量を超
えた液量の原廃水を−B′y貯留プる退避槽と、廃水処
理装置本体から流出する処理水の水質を計測する水質計
測器と、この水質計測器からの水質信号に基づいて上記
流量調節装置の送液量を制御する制御装置を具備したも
のであるので、時間的に変動する流入原廃水量を流量調
節装置で調節し、良好な処理水質が常時得られるような
聞の原廃水を処理装置本体に送液し、余剰の原廃水のみ
を退避槽に送ることができるため、退避槽に貯留される
原廃水量が少なくなり、よって退避槽を従来の流量調整
槽に比べて大幅に小型化でき、設備費用の低減を図るこ
とができる。また、処理水質によって処理装置本体への
原廃水の送液量を調節することができるので、処理水の
水質も安定するとともに放流水質の監視をも同時に行う
ことができるなどの利点を有するものである。
As explained above, the wastewater treatment device of the present invention includes a flow rate adjustment device that adjusts the amount of raw wastewater sent to the wastewater treatment device main body to a predetermined amount, and a flow rate adjustment device that adjusts the amount of liquid that exceeds the WI amount adjusted by the flow rate adjustment device. an evacuation tank for storing -B'y amount of raw wastewater; a water quality measuring device for measuring the quality of the treated water flowing out from the wastewater treatment equipment main body; and the above-mentioned flow rate adjustment device based on the water quality signal from this water quality measuring device. Since the system is equipped with a control device that controls the amount of liquid sent, the amount of raw wastewater that fluctuates over time can be adjusted using a flow rate adjustment device, and the raw wastewater can be treated in such a way that good treated water quality can always be obtained. Since the liquid can be sent to the equipment main body and only excess raw wastewater can be sent to the evacuation tank, the amount of raw wastewater stored in the evacuation tank is reduced, making the evacuation tank much smaller than a conventional flow rate adjustment tank. It is possible to reduce equipment costs. In addition, since the amount of raw wastewater sent to the treatment equipment can be adjusted depending on the quality of the treated water, the quality of the treated water is stabilized and the quality of the discharged water can be monitored at the same time. be.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来の廃水処理装置の例を示す概略構成図、第
2図は本発明の廃水処理装置を有機性廃水の活性汚泥に
よる生物処理に適用した場合の例を示す概略構成図であ
る。 11・・・・・・流量調節装置、12・・・・・・曝気
槽、13・・・・・・退避槽、17・・・・・・沈澱槽
、19・・・・・・汚泥界面J1.20・・・・・・監
視槽、21・・・・・・水質計測器、22・・・・・・
制御装置。 出願人 清水建設株式会社
FIG. 1 is a schematic configuration diagram showing an example of a conventional wastewater treatment device, and FIG. 2 is a schematic configuration diagram showing an example in which the wastewater treatment device of the present invention is applied to biological treatment using activated sludge of organic wastewater. . 11...Flow rate adjustment device, 12...Aeration tank, 13...Evacuation tank, 17...Sedimentation tank, 19...Sludge interface J1.20...Monitoring tank, 21...Water quality measuring instrument, 22...
Control device. Applicant: Shimizu Corporation

Claims (1)

【特許請求の範囲】 原廃水の廃水処理装置本体への送液量を所定量に調節す
る流量調節装置と、 この流量調節装置による調節量を超えた液量の原廃水を
一時貯留する退避槽と、 上記廃水処理装置本体から流出する処理水の水質を計測
する水質計測器と、 この水質計測器からの水質信号に基づいて上記流量調節
装置の送液量を制御する制御装置を具備したことを特徴
とする廃水処理装置。
[Scope of Claims] A flow rate adjustment device that adjusts the amount of raw wastewater sent to the wastewater treatment device main body to a predetermined amount, and an evacuation tank that temporarily stores the amount of raw wastewater that exceeds the amount regulated by the flow rate adjustment device. and a water quality measuring device for measuring the quality of treated water flowing out from the main body of the wastewater treatment device, and a control device for controlling the amount of liquid sent by the flow rate regulating device based on the water quality signal from the water quality measuring device. A wastewater treatment device featuring:
JP59061883A 1984-03-29 1984-03-29 Apparatus for treatment of waste water Pending JPS60206491A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59061883A JPS60206491A (en) 1984-03-29 1984-03-29 Apparatus for treatment of waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59061883A JPS60206491A (en) 1984-03-29 1984-03-29 Apparatus for treatment of waste water

Publications (1)

Publication Number Publication Date
JPS60206491A true JPS60206491A (en) 1985-10-18

Family

ID=13183982

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59061883A Pending JPS60206491A (en) 1984-03-29 1984-03-29 Apparatus for treatment of waste water

Country Status (1)

Country Link
JP (1) JPS60206491A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07275843A (en) * 1994-04-08 1995-10-24 Watanabe Consultants:Kk Operation control method for drainage treatment facility and central control system for more than one drainage treatment facility
WO2014034827A1 (en) * 2012-08-31 2014-03-06 東レ株式会社 Fresh water generation method

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5254262A (en) * 1975-10-28 1977-05-02 Fujisawa Pharmaceutical Co Waste water treating improved method by means of activated sludge method
JPS5775190A (en) * 1980-10-28 1982-05-11 Hitachi Plant Eng & Constr Co Ltd Method and device for automatic control of sewage treatment by activated sludge method
JPS59173196A (en) * 1983-03-19 1984-10-01 Meidensha Electric Mfg Co Ltd Sludge control device
JPS60153996A (en) * 1984-01-24 1985-08-13 Meidensha Electric Mfg Co Ltd Sludge control apparatus

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5254262A (en) * 1975-10-28 1977-05-02 Fujisawa Pharmaceutical Co Waste water treating improved method by means of activated sludge method
JPS5775190A (en) * 1980-10-28 1982-05-11 Hitachi Plant Eng & Constr Co Ltd Method and device for automatic control of sewage treatment by activated sludge method
JPS59173196A (en) * 1983-03-19 1984-10-01 Meidensha Electric Mfg Co Ltd Sludge control device
JPS60153996A (en) * 1984-01-24 1985-08-13 Meidensha Electric Mfg Co Ltd Sludge control apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07275843A (en) * 1994-04-08 1995-10-24 Watanabe Consultants:Kk Operation control method for drainage treatment facility and central control system for more than one drainage treatment facility
WO2014034827A1 (en) * 2012-08-31 2014-03-06 東レ株式会社 Fresh water generation method
JPWO2014034827A1 (en) * 2012-08-31 2016-08-08 東レ株式会社 Fresh water generation method

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