JP3452162B2 - Water quality control device - Google Patents
Water quality control deviceInfo
- Publication number
- JP3452162B2 JP3452162B2 JP28859595A JP28859595A JP3452162B2 JP 3452162 B2 JP3452162 B2 JP 3452162B2 JP 28859595 A JP28859595 A JP 28859595A JP 28859595 A JP28859595 A JP 28859595A JP 3452162 B2 JP3452162 B2 JP 3452162B2
- Authority
- JP
- Japan
- Prior art keywords
- control
- aeration
- water quality
- activated sludge
- process time
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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】
【0001】
【発明の属する技術分野】この発明は、排水中の窒素お
よびリンを生物学的に除去する回分式活性汚泥法の水質
制御装置に関するものである。
【0002】
【従来の技術】従来の排水中の窒素またはリン除去を行
う回分式活性汚泥法の水質制御装置は、攪拌および曝気
工程時間を運転管理者がタイマ等により手動で設定して
制御していた。しかしながら、回分槽内への流入水量お
よびその成分の変動により、タイマ制御だけでは常に最
適な制御を行うことは困難であった。
【0003】また、溶存酸素濃度(DO)または酸化還
元電位(ORP)等の水質計測機器を用いて制御を行う
場合も、DO計によるDO値の一定値制御、DO計およ
びORP計によるDOおよびORPの上限値制御が行わ
れていた。しかしながら、この場合も、1つの計測器に
より1つの値を制御する1入力1出力の制御であるの
で、計測器等の異常時には制御が困難であった。
【0004】また、特開平3−284398号公報に
は、連続流れ連続曝気式の下水処理の活性汚泥法におい
て、ORP計およびpH計により、送風量および曝気槽
のDOの目標値をファジィ推論を用いて制御する装置が
示されている。さらに、特開平5−31488号公報に
は、連続流れ間欠曝気式のし尿処理の活性汚泥法におい
て、DO,pH,ORPおよびアンモニア態または酸化
態窒素により、送風量および曝気時間をファジィ推論を
用いて制御する方法が示されている。しかしながら、こ
れらの技術は、連続流れ式の活性汚泥法について示され
たものであり、回分式活性汚泥法について何ら示された
ものではなく、攪拌工程時間の制御についても全く述べ
られていなかった。
【0005】
【発明が解決しようとする課題】従来の窒素またはリン
除去を行う回分式活性汚泥法の水質制御装置は以上のよ
うに構成されているので、タイマ制御では最適制御を行
うことは困難であり、また、水質計測機器を用いて制御
を行う場合も、計測器等の異常時には制御が困難であっ
た。また、水質計測機器を用いてファジィ制御を行う装
置もあるが、連続流れ式の活性汚泥法による装置であ
り、回分式活性汚泥法を対象としたものではないなどの
課題があった。
【0006】この発明は上記のような課題を解決するた
めになされたもので、水質計測機器を用いてファジィ制
御を行うことによって、攪拌工程時間および曝気工程時
間を最適制御する水質制御装置を得ることを目的とす
る。
【0007】
【課題を解決するための手段】この発明に係る回分式活
性汚泥法の水質制御装置は、回分槽内の溶存酸素濃度,
pHおよび酸化還元電位を計測する計測センサと、計測
した上記3種の計測値に基づいてファジィ推論により、
曝気用のブロアをオン・オフさせて回分槽における攪拌
工程時間および曝気工程時間を各々制御するファジィコ
ントローラとを備えたものである。
【0008】
【発明の実施の形態】実施の形態1.
以下、この発明の実施の一形態を説明する。図1はこの
発明の実施の形態1による窒素およびリン除去を行う回
分式活性汚泥法の水質制御装置を示す構成図であり、図
において、1は汚水処理施設に設けられた回分槽、2は
この回分槽1内に設けられ、汚水の溶存酸素濃度(D
O),pH,酸化還元電位(ORP)を計測する計測セ
ンサ、3はこの計測センサ2の計測値に基づいてファジ
ィ推論により、ブロワ4をオン・オフし、回分槽1の攪
拌および曝気工程時間を制御するファジィコントローラ
である。なお、計測センサ2は、これらの計測値に加え
て回分槽1の水位を計測し、制御に加えてもよい。ま
た、回分槽1への流入水量が少なく、曝気工程時間だけ
で制御できない時は、送風量を制御してもよい。
【0009】次に動作について説明する。図2は計測セ
ンサ2で計測されたDO,pH,ORPの3種の計測値
に基づいて、ファジィコントローラ3がファジィ推論に
より、ブロワ4をオン・オフ制御した時の回分槽1の攪
拌および曝気工程時間を示したものである。
【0010】図3は回分式活性汚泥法でのタイマ制御と
ファジィ制御の実験結果を比較したものであり、タイマ
制御とファジィ制御を比べると、窒素除去率が67%か
ら91%と大幅に向上し、リン除去率も58%から79
%と向上した。このように、ファジィコントローラ3に
より回分槽1の攪拌および曝気工程時間を最適制御した
結果、より高効率の窒素およびリン除去が可能になっ
た。また、この実施の形態の装置は、窒素除去またはリ
ン除去のみが必要とされる場合にも適用できることは言
うまでもない。なお、この実施の形態において、連続計
測可能な計測センサ2を用いているので、ファジィコン
トローラ3による回分槽1の攪拌および曝気工程時間を
例えば1分毎にファジィ推論することができ、また、3
種の計測値に基づいて回分槽1の攪拌および曝気工程時
間を制御しているので、攪拌および曝気工程時間をより
細かく最適に制御することができた。
【0011】
【発明の効果】以上のように、この発明によれば、回分
槽内の溶存酸素濃度,pHおよび酸化還元電位を計測す
る計測センサの3種の計測値に基づいてファジィ推論に
より、攪拌および曝気工程時間を各々制御するファジィ
コントローラを備えるように構成したので、回分槽内へ
の流入水量およびその成分が変動しても、攪拌および曝
気工程時間を最適制御することができ、排水中の窒素お
よびリンをより高効率に除去することができる効果があ
る。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention, water quality control system of batch-type activated sludge process to remove the nitrogen your <br/> by beauty Li down in the wastewater biologically It is about. [0002] The nitrogen Motoma other in conventional wastewater quality control system for batchwise activated sludge method in which phosphorus removal, stirring and aeration process time operation administrator set manually by a timer or the like Had control. However, due to fluctuations in the amount of water flowing into the batch tank and its components, it has been difficult to always perform optimal control only by timer control. [0003] Further, when control is performed using a water quality measuring device such as a dissolved oxygen concentration (DO) or an oxidation-reduction potential (ORP), the DO value is controlled by a DO meter and the DO and ORP meters are controlled by a constant value. ORP upper limit control was performed. However, also in this case, the control is one-input and one-output, in which one value is controlled by one measuring device, so that it is difficult to control when the measuring device or the like is abnormal. Japanese Patent Application Laid-Open No. 3-284398 discloses a fuzzy inference of the air flow rate and the target value of DO in an aeration tank by an ORP meter and a pH meter in an activated sludge method of sewage treatment in a continuous flow continuous aeration system. An apparatus to be used and controlled is shown. Further, Japanese Patent Application Laid-Open No. 5-31488 discloses that, in an activated sludge method for continuous-flow intermittent aeration type night soil treatment, the amount of air blown and the aeration time are determined by fuzzy inference using DO, pH, ORP, and ammonium or oxidized nitrogen. A control method is shown. However, these techniques have been described for a continuous flow activated sludge process, not for a batch activated sludge process, and have no mention of controlling the stirring step time. [0005] Since INVENTION Problems to be Solved conventional nitrogen Motoma other water quality control system for batchwise activated sludge method involving phosphorus removal is constructed as described above, performs optimum control in timer control This is difficult, and when control is performed using a water quality measuring device, it is difficult to control when the measuring device or the like is abnormal. In addition, there is a device that performs fuzzy control using a water quality measuring device, but there is a problem that the device is based on a continuous flow activated sludge method and is not intended for a batch activated sludge method. SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and provides a water quality control device that optimally controls a stirring process time and an aeration process time by performing fuzzy control using a water quality measuring device. The purpose is to: [0007] A water quality control apparatus for a batch type activated sludge method according to the present invention comprises:
Based on a measurement sensor that measures pH and oxidation-reduction potential, and fuzzy inference based on the above three measured values,
A fuzzy controller for turning on and off the blower for aeration and controlling the stirring process time and the aeration process time in the batch tank, respectively , is provided. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS First Embodiment Hereinafter, an embodiment of the present invention will be described. Figure 1 is a block diagram showing a water quality control system for batchwise activated sludge method involving nitrogen and Li emissions removed according to the first embodiment of the present invention. In the figure, 1 is batch tank provided in wastewater treatment facilities , 2 are provided in the batch tank 1 and the dissolved oxygen concentration (D
O), pH, a measurement sensor for measuring the oxidation-reduction potential (ORP), 3 turns on / off the blower 4 by fuzzy inference based on the measurement value of the measurement sensor 2, and agitates the batch tank 1 and aeration process time. it is a fuzzy controller to control. Na us, measuring sensor 2, the water level of the added batch tank 1 to these measured values are measured, may be added to the control. Further, when the amount of water flowing into the batch tank 1 is small and cannot be controlled only by the aeration step time, the amount of air blown may be controlled. Next, the operation will be described. FIG. 2 shows stirring and aeration of the batch tank 1 when the fuzzy controller 3 controls the blower 4 on / off by fuzzy inference based on three kinds of measured values of DO, pH and ORP measured by the measuring sensor 2. It shows the process time. FIG. 3 is a comparison of experimental results of timer control and fuzzy control in the batch activated sludge method. Compared with timer control and fuzzy control, the nitrogen removal rate is greatly improved from 67% to 91%. And the phosphorus removal rate is 58% to 79%.
%. As described above, the fuzzy controller 3 optimally controls the stirring and the aeration process time of the batch tank 1, so that nitrogen and phosphorus removal can be performed with higher efficiency. Further, it goes without saying that the apparatus of this embodiment can be applied to a case where only nitrogen removal or phosphorus removal is required. Incidentally, in this embodiment, because of the use of continuous measurement possible measuring sensor 2, it is possible to fuzzy inference stirring and aeration process time of the fuzzy controller 3 by batch tank 1, for example every minute, also, 3
Since the stirring and aeration step times of the batch tank 1 are controlled based on the measured values of the species , the stirring and aeration step times could be more finely and optimally controlled. As described above, according to the present invention, fuzzy inference is performed based on three types of measurement values of a measurement sensor for measuring dissolved oxygen concentration, pH and oxidation-reduction potential in a batch tank. since it is configured to include a fuzzy controller for controlling each of the agitation and aeration process time, be varied inflow water and its components to the batch tank, it is possible to optimally control the agitation and aeration process time, the waste water Nitrogen and phosphorus can be more efficiently removed.
【図面の簡単な説明】
【図1】この発明の実施の形態1による窒素およびリン
除去を行う回分式活性汚泥法の水質制御装置を示す構成
図である。
【図2】ファジィコントローラによる制御状況を示す特
性図である。
【図3】回分式活性汚泥法でのタイマ制御とファジィ制
御の実験結果を比較した表図である。
【符号の説明】
1 回分槽
2 計測センサ
3 ファジィコントローラBRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a block diagram showing a water quality control system for batchwise activated sludge method involving nitrogen and Li emissions removed according to a first embodiment of the invention. FIG. 2 is a characteristic diagram showing a control situation by a fuzzy controller. FIG. 3 is a table chart comparing experimental results of timer control and fuzzy control in the batch activated sludge method. [Explanation of symbols] Single batch tank 2 Measurement sensor 3 Fuzzy controller
フロントページの続き (56)参考文献 特開 平5−31488(JP,A) 特開 平6−91294(JP,A)Continuation of front page (56) References JP-A-5-31488 (JP, A) JP-A-6-91294 (JP, A)
Claims (1)
化還元電位を計測する計測センサと、 計測した上記3種の計測値に基づいてファジィ推論によ
り、曝気用ブロアをオン・オフさせて、回分槽における
攪拌工程時間および曝気工程時間を各々制御するファジ
ィコントローラとを備えた窒素およびリン除去を行う回
分式活性汚泥法の水質制御装置。(57) [Claims] [Claim 1] A measurement sensor for measuring the concentration of dissolved oxygen, pH, and oxidation-reduction potential in a batch tank, and aeration is performed by fuzzy inference based on the above three measured values. the use blower are turned on and off, batch tank stirring process time and the aeration process time quality control system for batchwise activated sludge method in which nitrogen and phosphorus removal and a fuzzy controller for controlling each of the.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28859595A JP3452162B2 (en) | 1995-11-07 | 1995-11-07 | Water quality control device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28859595A JP3452162B2 (en) | 1995-11-07 | 1995-11-07 | Water quality control device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH09122681A JPH09122681A (en) | 1997-05-13 |
JP3452162B2 true JP3452162B2 (en) | 2003-09-29 |
Family
ID=17732289
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP28859595A Expired - Fee Related JP3452162B2 (en) | 1995-11-07 | 1995-11-07 | Water quality control device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3452162B2 (en) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2779140B1 (en) * | 1998-06-02 | 2001-01-05 | Suez Lyonnaise Des Eaux | METHOD FOR CONTROLLING AERATION IN A BIOLOGICAL WASTEWATER TREATMENT PLANT |
KR100338510B1 (en) * | 1999-07-16 | 2002-05-30 | 라창식 | Real-time control technology for wastewater treatment system |
JP2002307095A (en) * | 2001-04-17 | 2002-10-22 | Mitsubishi Heavy Ind Ltd | Wastewater treatment facility |
KR100424999B1 (en) * | 2002-03-19 | 2004-03-27 | 주식회사 한스환경엔지니어링 | Controlling system and method of sequencing batch reactor |
FR2858609B1 (en) * | 2003-08-04 | 2006-10-13 | Otv Sa | METHOD AND INSTALLATION FOR BIOLOGICAL TREATMENT OF ACTIVATED SLUDGE WATER WITH AERATION CONTROL |
WO2005068379A1 (en) * | 2004-01-13 | 2005-07-28 | Itochu Forestry Corp. | Wastewater cleaning system |
FR2889180B1 (en) * | 2005-08-01 | 2008-04-04 | Suez Environnement Sa | PROCESS AND PLANT FOR TREATING NITROGEN CONCENTRATE EFFLUENTS IN A FRACTIONAL CYCLE SEQUENTIAL BIOLOGICAL REACTOR |
CN103570190B (en) * | 2013-10-20 | 2015-04-29 | 北京化工大学 | Method for controlling feeding amount of chemical phosphorus removal reagents of water reclamation plants based on fuzzy control |
-
1995
- 1995-11-07 JP JP28859595A patent/JP3452162B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH09122681A (en) | 1997-05-13 |
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