JPH0389993A - Method for controlling concentration of phosphorus in waste water - Google Patents

Method for controlling concentration of phosphorus in waste water

Info

Publication number
JPH0389993A
JPH0389993A JP1224352A JP22435289A JPH0389993A JP H0389993 A JPH0389993 A JP H0389993A JP 1224352 A JP1224352 A JP 1224352A JP 22435289 A JP22435289 A JP 22435289A JP H0389993 A JPH0389993 A JP H0389993A
Authority
JP
Japan
Prior art keywords
flocculant
phosphorus
amount
treated water
water
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.)
Granted
Application number
JP1224352A
Other languages
Japanese (ja)
Other versions
JPH06102195B2 (en
Inventor
Kazuaki Sato
和明 佐藤
Masashi Ogoshi
小越 真佐司
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.)
Minister for Public Works for State of New South Wales
National Research and Development Agency Public Works Research Institute
Original Assignee
Minister for Public Works for State of New South Wales
Public Works Research Institute Ministry of Construction
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 Minister for Public Works for State of New South Wales, Public Works Research Institute Ministry of Construction filed Critical Minister for Public Works for State of New South Wales
Priority to JP1224352A priority Critical patent/JPH06102195B2/en
Publication of JPH0389993A publication Critical patent/JPH0389993A/en
Publication of JPH06102195B2 publication Critical patent/JPH06102195B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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

  • Removal Of Specific Substances (AREA)
  • Activated Sludge Processes (AREA)

Abstract

PURPOSE:To control the concn. of phosphorus in treated water constant by calculating the estimated quantity value of the phosphorus removing quantity of this water treatment process on the basis of the change of the detected phosphorus concentration value of treated water and controlling the addition amount of a flocculant so as to eliminate the fluctuation of phosphorus removing quantity. CONSTITUTION:A flocculant injection point 2 is provided to an aeration tank 1 and a detection point 4 and a treated water outflow port 5 are provided to a final sedimentation tank and phosphorus in the water to be inspected collected at the detection point 4 is monitored by a colorimetric phosphorus detector 6 and a concn. signal is inputted to a program type operational controller 7. The program type operational controller 7 sends a pump control signal to a flocculant injection pump 8 so as to inject an estimated amount of a flocculant and a controlled amount of the flocculant is sent to the flocculant injection point 2 from a flocculant storage tank 9 by the flocculant injection pump 8. Even when there are the difference in biological dephosphorizing capacity and the difference in natural environment, a proper amount of the flocculant can be always supplied and, therefore, phosphorus in waste water can be effectively removed by the min. injection of the flocculant.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は水処理特に排水の処理に、化学凝集剤を用いて
処理水のリンを除去する処理方法又は生物的水処理法、
所謂活性汚泥法およびその各種変法において凝集剤を添
加して処理水のリンを除去する方法において、処理水の
リン濃度に応じた適量の凝集剤で排水中のリン除去を効
率よく行う方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a treatment method for water treatment, particularly wastewater treatment, in which phosphorus is removed from treated water using a chemical coagulant, or a biological water treatment method;
This invention relates to a method of efficiently removing phosphorus from wastewater by adding a flocculant to remove phosphorus from treated water in the so-called activated sludge method and its various modifications using an appropriate amount of flocculant depending on the phosphorus concentration of the treated water. .

〔従来の技術〕[Conventional technology]

生活、工業上からの排水中のリンを処理する方法として
は、従来、生物的脱リン作用を利用した所謂嫌気・好気
活性汚泥法が行われているが、生物的作用のみに依存す
ると排水中のB○D(生物学的酸素要求量)の濃度の変
化によって充分な脱リン機能が得られない場合があるの
で、現在はこの生物的脱リン作用によらず、凝集剤を併
用してリンの除去を行う活性汚泥法の各種の変法、例え
ば凝集剤添加循環式硝化脱窒法、凝集剤添加活性汚泥法
等も行われている。
Conventionally, the so-called anaerobic/aerobic activated sludge method, which utilizes biological dephosphorization, has been used to treat phosphorus in wastewater from domestic and industrial sources. Because sufficient dephosphorization function may not be obtained due to changes in the concentration of B○D (biological oxygen demand) in Various modified methods of the activated sludge method for removing phosphorus, such as the flocculant-added circulating nitrification-denitrification method and the flocculant-added activated sludge method, have also been carried out.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

上記活性汚泥法に凝集剤の添加を併用した排水の脱リン
法においては、凝集剤の添加により発生汚泥量が増大す
る欠点があるため、下水処理場においては生物的な脱リ
ン法が適していると考えられている。しかし、生物的な
脱リン法では生物の必要とするBOD濃度が低下した場
合に、脱リン機能が低下してリン除去が不安定になる。
The above-mentioned activated sludge method combined with the addition of a flocculant has the disadvantage that the amount of sludge generated increases, so biological dephosphorization is suitable for sewage treatment plants. It is believed that there are. However, in biological dephosphorization methods, when the BOD concentration required by living organisms decreases, the dephosphorization function decreases and phosphorus removal becomes unstable.

そこで、この生物的な脱リン法に凝集剤による脱リン作
用を組み合せた方法が研究されたが、リンの含量の不安
定な処理用水にどの程度の凝集剤量を添加するかが非常
に困難な点であった。
Therefore, research has been conducted on a method that combines this biological dephosphorization method with the dephosphorization effect of a flocculant, but it is extremely difficult to determine how much flocculant to add to the treated water, which has an unstable phosphorus content. That was the point.

この問題点を解決するには、生物的脱リンによる除去程
度を予測して適正な凝集剤量を添加するか、処理後の水
の処理結果を分析して、この値から適正な凝集剤の添加
量を定めるかの何れかの方法が考えられるが、前者の方
法においては、生物的脱リンの機構が十分に解明されて
いない現状では不可能であり、後者の方法においては、
水の処理結果の分析に約1時開度度の時間を要し、これ
より凝集剤添加の調整結果を得るまでに更にかなりの時
間を要し、流入処理時に水のリン濃度に応じた量を加え
ることはできなかった。また、活性汚泥を用いるプロセ
スに凝集剤を添加する場合にあっては、添加した凝集剤
によるリン除去効果の発現が活性汚泥中の凝集剤濃度の
上昇を待って行なわれると考えられたため、短時間の変
動に対して凝集剤注入量の変化でこれを抑制しようとす
る場合には膨大な量の凝集剤を増減しなければならず、
実際的ではないと考えられていた。
To solve this problem, either predict the degree of removal by biological dephosphorization and add an appropriate amount of flocculant, or analyze the treatment results of the treated water and use this value to determine the appropriate amount of flocculant. One method is to determine the amount of addition, but the former method is impossible at present because the mechanism of biological dephosphorization has not been fully elucidated, and the latter method:
It takes about 1 hour to analyze the water treatment results, and it takes a considerable amount of time to obtain the results of adjusting the flocculant addition. could not be added. In addition, when adding a flocculant to a process using activated sludge, it was thought that the phosphorus removal effect of the added flocculant would take place after the concentration of flocculant in the activated sludge increased. If you try to suppress this by changing the amount of coagulant injected in response to time fluctuations, you will have to increase or decrease a huge amount of coagulant.
It was considered impractical.

本発明は、凝集剤の添加による水処理法において、適切
な注入位置を選択することにより、処理水のリンの濃度
から、プロセス全体のリン除去量の過不足値を予測して
適正の量の凝集剤を添加しプロセスのリン除去量の過不
足を補うことにより処理水のリン濃度を一定に制御する
方法を提供することを目的とするものである。
In a water treatment method by adding a flocculant, the present invention predicts the excess or deficiency of the amount of phosphorus removed in the entire process from the phosphorus concentration of the treated water by selecting an appropriate injection position, and then selects the appropriate amount. The object of the present invention is to provide a method for controlling the phosphorus concentration of treated water to a constant level by adding a flocculant to compensate for excess or deficiency in the amount of phosphorus removed in the process.

〔課題を解決するための手段〕[Means to solve the problem]

本発明は排水中の溶解性リンの除去を、化学凝集作用、
または生物的作用と化学凝集作用との併用によって行う
水処理プロセスにおいて、添加する凝集剤量を、リン検
出器により検出された処理水のリン濃度値の変化に基づ
いて本処理水プロセスのリン除去量の過不足予測値を算
定し、リン除去量の過不足をなくすよう凝集剤添加量を
制御することにより排水のリン濃度の制御を適正に行う
方法である。
The present invention removes soluble phosphorus from wastewater by chemical coagulation,
Or, in a water treatment process that uses a combination of biological action and chemical flocculation, the amount of flocculant to be added is determined based on the change in the phosphorus concentration value of the treated water detected by a phosphorus detector. This is a method for appropriately controlling the phosphorus concentration of wastewater by calculating the predicted value of excess or deficiency in the amount of phosphorus removed, and controlling the amount of coagulant added so as to eliminate excess or deficiency in the amount of phosphorus removed.

本発明の排水は主として溶解性リンの多い生活排水に使
用されるが、その他の排水例えば工業排水にも利用する
ことができる。
Although the wastewater of the present invention is mainly used for domestic wastewater containing a large amount of soluble phosphorus, it can also be used for other wastewater such as industrial wastewater.

本発明の方法は、排水の化学凝集作用または、生物的作
用と化学凝集作用を併用した排水処理プロセスに使用さ
れる。特に、生物的作用と化学凝集作用を併用した排水
処理プロセスに適用すれば一層良好な効果が得られる。
The method of the present invention is used in a wastewater treatment process that uses chemical flocculation of wastewater or a combination of biological and chemical flocculation. In particular, even better effects can be obtained if applied to a wastewater treatment process that uses both biological action and chemical flocculation action.

本発明の方法は、排水処理システムの最終段の処理水に
リン検出器例えば比色分析法、イオ5 ン電極法又はプラズマ発光分析法による検出器、特に比
色分析法による検出器を用いて、制御周期初めのリン濃
度(PO)を測定し、一定時間(b)後のリン濃度(P
l)を測定し、リン濃度の一定時間の変化率(d) d
 = (P +  Po) / bを算出し、この変化
率を基にして、遡り予測時間Cのリン濃度の予測値(P
c)を変化率dと予測時間Cの関数Pc=f(d、c)
により算出する。関数f(d、c)が最も単純な場合は
Pc=P、+d−cとなる。
The method of the present invention uses a phosphorus detector such as a colorimetric method, an ion electrode method, or a plasma emission spectrometry detector, particularly a colorimetric detector, to treat water in the final stage of a wastewater treatment system. , the phosphorus concentration (PO) at the beginning of the control cycle is measured, and the phosphorus concentration (P
l) and the rate of change in phosphorus concentration over a certain period of time (d) d
= (P + Po) / b is calculated, and based on this rate of change, the predicted value of phosphorus concentration (P
c) as a function of the rate of change d and the predicted time C Pc = f (d, c)
Calculated by When the function f(d, c) is the simplest, Pc=P, +d−c.

次に、以上の如くして得られた算出値(Pc)と制御の
目標とする処理リン濃度目標値(S)の差(e)e=P
c−3を算出し、この差(e)に適合した(e)の関数
g (e)で算出されるリン凝集剤、例えば硫酸アルミ
ニウムの適量(i) i=g(e)を増減して注入する
Next, the difference (e) between the calculated value (Pc) obtained as above and the target value (S) of the phosphorus concentration to be controlled, e=P
Calculate c-3 and calculate the appropriate amount of phosphorus flocculant, e.g. aluminum sulfate (i) by increasing or decreasing i=g(e) inject.

このリン濃度検出、演算、凝集剤の注入量の増減は全て
自動制御によって行うことができる。
This phosphorus concentration detection, calculation, and increase/decrease in the amount of coagulant to be injected can all be performed by automatic control.

また、活性汚泥を用いるプロセスに凝集剤を添加する場
合にあっては、凝集剤の注入位置を活性汚泥処理の最終
段から最終固液分離装置にいたる流路内で、かつ添加し
た凝集剤が十分な攪拌混合を受けることができる位置と
することによって、活性汚泥中の凝集剤濃度の変化によ
らず、注入凝集剤濃度の変化に応じて処理水リン濃度の
制御を行なうことができ、上記制御手法を適用すること
ができる。
In addition, when adding a flocculant to a process using activated sludge, the injection position of the flocculant should be placed within the flow path from the final stage of activated sludge treatment to the final solid-liquid separation device, and the added flocculant By setting the position so that it can receive sufficient stirring and mixing, the phosphorus concentration in the treated water can be controlled according to changes in the injected flocculant concentration, regardless of changes in the flocculant concentration in the activated sludge. Control techniques can be applied.

以上の本発明の方法を用いることによって、流入される
排水のリン濃度の変化に即応した量の凝集剤を注入する
ことができ、また、生物的作用と化学的作用を併用する
場合においても、生物の脱リン機能の高低によっても凝
集剤の注入量が制御できる。
By using the method of the present invention described above, it is possible to inject an amount of flocculant that immediately responds to changes in the phosphorus concentration of incoming wastewater, and even when using both biological and chemical effects, The amount of coagulant to be injected can also be controlled depending on the level of the dephosphorization function of the organism.

次に本発明の実施例を挙げ、本発明を更に詳細に説明す
るが、本発明はこの実施例に限定されるものではないこ
とは言うまでもない。
EXAMPLES Next, the present invention will be described in more detail with reference to Examples, but it goes without saying that the present invention is not limited to these Examples.

〔実施例〕〔Example〕

容積200ホの曝気槽(1)に凝集剤(硫酸アルミニウ
ム)注入点(2)を有し、最終沈澱槽(3)に検出点(
4)及び処理水流出口(5)を備えた、排水処理システ
ムにおいて、検出点より採取された検=7 水を比色式のリン検出器(6)により、リンをモニター
し、この濃度信号をプログラム式演算制御器(横滑電機
■製、SCMS型)(7)により凝集剤注入ポンプ(8
)の注入量を凝集剤予測量を注入するようにポンプの稼
動を制御するポンプ制御信号を凝集剤注入ポンプ(8)
に送り、同ポンプの凝集剤貯槽(9)から制御された量
の凝集剤を凝集剤注入点(2)に送り込む排水処理シス
テム(第1図で示す)において、流入水を480m/d
で6月始めから10月の終りまでの各時期I、I[、I
II (A−1,A−2,B−1,B2及びC)の流入
水(INF)を流し、流入水及び処理後の処理水(EF
F)の溶解性リン(PD)、総窒素(T−N)、生物学
的酸素要求量(BOD)並びに処理に用した凝集剤(硫
酸アルミニウム)の注入率を測定した(第1表参照)。
The aeration tank (1) with a capacity of 200 mm has a flocculant (aluminum sulfate) injection point (2), and the final settling tank (3) has a detection point (
In a wastewater treatment system equipped with 4) and a treated water outlet (5), a colorimetric phosphorus detector (6) monitors the phosphorus in the water sampled from the detection point (=7), and the concentration signal is recorded. A programmable arithmetic controller (manufactured by Yokoguri Denki ■, SCMS type) (7) is used to control the coagulant injection pump (8).
) to the flocculant injection pump (8).
In a wastewater treatment system (shown in Figure 1) that pumps a controlled amount of flocculant from the flocculant storage tank (9) of the same pump to the flocculant injection point (2), the inflow water is pumped at a rate of 480 m/d.
For each period from the beginning of June to the end of October, I, I [, I
II (A-1, A-2, B-1, B2 and C), the influent water (INF) and the treated water after treatment (EF
F) Soluble phosphorus (PD), total nitrogen (T-N), biological oxygen demand (BOD), and the injection rate of the flocculant (aluminum sulfate) used in the treatment were measured (see Table 1). .

これを流入水と処理水とのリン濃度について図で示すと
第2図の通りである。
This is illustrated in Figure 2 with respect to the phosphorus concentrations of inflow water and treated water.

第 表 〔発明の効果〕 本発明は生物の脱リン能力の相違、その他の天然環境の
差異があっても、常に適正な量の凝集剤を供給できるか
ら、最少限の凝集剤の注入で有効に排水中のリンを除く
ことを可能にする方法である。従って排水による閉鎖性
水域へのリンの負荷量削減に極めて有用な発明である。
Table [Effects of the Invention] The present invention can always supply an appropriate amount of flocculant even if there are differences in the dephosphorization ability of living organisms or other differences in the natural environment, so it is effective with the minimum injection of flocculant. This method makes it possible to remove phosphorus from wastewater. Therefore, this invention is extremely useful for reducing the amount of phosphorus loaded into closed water bodies due to wastewater.

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

第1図は本発明の排水処理システムの工程図、第2図は
、実施例の流入水と処理水とのリン濃度を表わした図面
である。 図中、1は曝気槽、2は凝集剤注入点、3は最終沈澱槽
、4は検出点、5は排水処理出口、6はリン検出器、7
は凝集剤注入量制御装置、8は凝集剤注入ポンプ、9は
凝集剤貯槽を示す。 0
FIG. 1 is a process diagram of the wastewater treatment system of the present invention, and FIG. 2 is a drawing showing the phosphorus concentrations of inflow water and treated water in an example. In the figure, 1 is an aeration tank, 2 is a flocculant injection point, 3 is a final settling tank, 4 is a detection point, 5 is a wastewater treatment outlet, 6 is a phosphorus detector, and 7
8 shows a flocculant injection amount control device, 8 a flocculant injection pump, and 9 a flocculant storage tank. 0

Claims (1)

【特許請求の範囲】 1、排水中の溶解性リンの除去を、化学凝集作用、また
は生物的作用と化学凝集作用との併用によって行う水処
理プロセスにおいて、添加する凝集剤量を、リン検出器
により検出された処理水リン濃度値の変化に基づいて本
水処理プロセスのリン除去量の過不足予測値を算定し、
リン除去量の過不足を失くすよう制御することを特徴と
する排水のリン濃度制御方法。 2、リン濃度の制御法を活性汚泥法及びその各種の変法
と凝集剤との併用プロセスに対して適用する場合にあっ
て、凝集剤の注入位置を活性汚泥処理の最終段から最終
固液分離装置にいたる流路内で、かつ添加した凝集剤が
十分な攪拌混合を受けることができる位置とする請求項
1の排水のリン濃度制御方法。
[Claims] 1. In a water treatment process in which soluble phosphorus in wastewater is removed by chemical flocculation or a combination of biological and chemical flocculation, the amount of flocculant to be added is measured using a phosphorus detector. Calculate the predicted excess or deficiency of the amount of phosphorus removed in this water treatment process based on the change in the phosphorus concentration value of the treated water detected by
A method for controlling the concentration of phosphorus in wastewater, characterized by controlling the amount of phosphorus removed to eliminate excess or deficiency. 2. When applying the phosphorus concentration control method to a process that uses the activated sludge method or its various modified methods in combination with a flocculant, the injection position of the flocculant should be changed from the final stage of activated sludge treatment to the final solid liquid. 2. The method for controlling phosphorus concentration in wastewater according to claim 1, wherein the location is within the flow path leading to the separator and where the added flocculant can receive sufficient stirring and mixing.
JP1224352A 1989-09-01 1989-09-01 Method for controlling phosphorus concentration in wastewater Expired - Lifetime JPH06102195B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1224352A JPH06102195B2 (en) 1989-09-01 1989-09-01 Method for controlling phosphorus concentration in wastewater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1224352A JPH06102195B2 (en) 1989-09-01 1989-09-01 Method for controlling phosphorus concentration in wastewater

Publications (2)

Publication Number Publication Date
JPH0389993A true JPH0389993A (en) 1991-04-15
JPH06102195B2 JPH06102195B2 (en) 1994-12-14

Family

ID=16812424

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1224352A Expired - Lifetime JPH06102195B2 (en) 1989-09-01 1989-09-01 Method for controlling phosphorus concentration in wastewater

Country Status (1)

Country Link
JP (1) JPH06102195B2 (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001353496A (en) * 2000-06-12 2001-12-25 Toshiba Corp Sewage disposal system and measuring system
JP2005125152A (en) * 2003-10-21 2005-05-19 Kurita Water Ind Ltd Water treatment method and water treatment apparatus
WO2009004123A1 (en) * 2007-07-05 2009-01-08 Biolan Oy Apparatus and method for precipitation of phosphorus from waste water
JP2010005623A (en) * 2009-10-09 2010-01-14 Mitsubishi Electric Corp Controller for biological water treating apparatus
JP2013039576A (en) * 2012-11-29 2013-02-28 Mitsubishi Electric Corp Controller for biological water treating apparatus
JP2014147936A (en) * 2014-05-26 2014-08-21 Mitsubishi Electric Corp Controller for biological water treatment apparatus
JP2014147935A (en) * 2014-05-26 2014-08-21 Mitsubishi Electric Corp Controller for biological water treatment apparatus
JP2014176849A (en) * 2014-05-26 2014-09-25 Mitsubishi Electric Corp Controller for biological water treatment device
WO2020170364A1 (en) * 2019-02-20 2020-08-27 三菱電機株式会社 Water treatment apparatus and water treatment method

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001353496A (en) * 2000-06-12 2001-12-25 Toshiba Corp Sewage disposal system and measuring system
JP2005125152A (en) * 2003-10-21 2005-05-19 Kurita Water Ind Ltd Water treatment method and water treatment apparatus
JP4543656B2 (en) * 2003-10-21 2010-09-15 栗田工業株式会社 Water treatment method and water treatment apparatus
WO2009004123A1 (en) * 2007-07-05 2009-01-08 Biolan Oy Apparatus and method for precipitation of phosphorus from waste water
JP2010005623A (en) * 2009-10-09 2010-01-14 Mitsubishi Electric Corp Controller for biological water treating apparatus
JP2013039576A (en) * 2012-11-29 2013-02-28 Mitsubishi Electric Corp Controller for biological water treating apparatus
JP2014147936A (en) * 2014-05-26 2014-08-21 Mitsubishi Electric Corp Controller for biological water treatment apparatus
JP2014147935A (en) * 2014-05-26 2014-08-21 Mitsubishi Electric Corp Controller for biological water treatment apparatus
JP2014176849A (en) * 2014-05-26 2014-09-25 Mitsubishi Electric Corp Controller for biological water treatment device
WO2020170364A1 (en) * 2019-02-20 2020-08-27 三菱電機株式会社 Water treatment apparatus and water treatment method

Also Published As

Publication number Publication date
JPH06102195B2 (en) 1994-12-14

Similar Documents

Publication Publication Date Title
US8916046B2 (en) Method for controlling oxygen supply for treating wastewater, and facility for implementing same
JPH0389993A (en) Method for controlling concentration of phosphorus in waste water
JP2002126779A (en) Sludge treatment method and apparatus used therefor
JPH0938690A (en) Method for controlling injection of flocculating agent in water treatment
JP5854743B2 (en) Operation control device and control method for sewage treatment plant
JP3058414B1 (en) Water treatment equipment
JPH07115025B2 (en) Bulking control method using SVI
JPH07299495A (en) Nitrification accelerating method for activated sludge circulation modulating method and method for predicting nitrification rate
JPH11262777A (en) Method for removing phosphorus in wastewater
JPH09122681A (en) Water quality controlling apparatus
JP4364955B2 (en) Operation control method of aeration equipment and sludge extraction pump
JP3724694B2 (en) Biological treatment method and equipment for organic wastewater
JP3763551B2 (en) Water treatment system
CZ20011213A3 (en) Enhancement of sewage treatment process by making use of activated sludge purification method
JP3376620B2 (en) Biological denitrification treatment apparatus and biological denitrification treatment method
JP2003154388A (en) Organic matter injection apparatus
JP2002119991A (en) Method for adjusting activated sludge, and method and apparatus for treating organic wastewater using the same
JPH04166295A (en) Activated sludge process by srt control
JP2001038381A (en) Method for removing phosphorus in waste water
JPH03262599A (en) Purification for removing nitrogen and phosphorus in polluted water
JP2001314889A (en) Method for controlling biological removal of phosphorus from wastewater
JPH034994A (en) Sewage treating apparatus
JP2899807B2 (en) Method and apparatus for treating polluted water
JPS6134879B2 (en)
JPH11300382A (en) Method for removing phosphorus in sewage

Legal Events

Date Code Title Description
EXPY Cancellation because of completion of term