JPH0141111B2 - - Google Patents

Info

Publication number
JPH0141111B2
JPH0141111B2 JP15532580A JP15532580A JPH0141111B2 JP H0141111 B2 JPH0141111 B2 JP H0141111B2 JP 15532580 A JP15532580 A JP 15532580A JP 15532580 A JP15532580 A JP 15532580A JP H0141111 B2 JPH0141111 B2 JP H0141111B2
Authority
JP
Japan
Prior art keywords
water
turbidity
sludge
over time
treated 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.)
Expired
Application number
JP15532580A
Other languages
Japanese (ja)
Other versions
JPS5778991A (en
Inventor
Takao Sekine
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.)
Meidensha Electric Manufacturing Co Ltd
Original Assignee
Meidensha Electric Manufacturing 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 Meidensha Electric Manufacturing Co Ltd filed Critical Meidensha Electric Manufacturing Co Ltd
Priority to JP15532580A priority Critical patent/JPS5778991A/en
Publication of JPS5778991A publication Critical patent/JPS5778991A/en
Publication of JPH0141111B2 publication Critical patent/JPH0141111B2/ja
Granted 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

  • Treatment Of Biological Wastes In General (AREA)
  • Activated Sludge Processes (AREA)

Description

【発明の詳細な説明】 本発明は、活性汚泥処理や浄水プロセスの沈殿
池における固液分離の状態監視ならびに上澄水質
の予測制御のための水質監視制御方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a water quality monitoring and control method for monitoring the state of solid-liquid separation in a settling tank in activated sludge treatment and water purification processes, and for predictive control of supernatant water quality.

活性汚泥処理プロセスにおいて、最終沈殿池で
は活性汚泥と処理水に固液分離されるが、この沈
降特性の指標として従来から30分汚泥容量SV30
や汚泥容量指標SVIが用いられその自動測定装置
も開発されている。しかし、この従来の固液分離
状態監視では次のような欠点がある。
In the activated sludge treatment process, activated sludge and treated water are separated into solid and liquid in the final settling tank, and as an indicator of the settling characteristics, the 30 minute sludge volume SV 30 has traditionally been used as an indicator of the settling characteristics.
The sludge volume index SVI is used, and an automatic measuring device has also been developed. However, this conventional solid-liquid separation state monitoring has the following drawbacks.

(1) SVIが小さい場合、即ち活性汚泥の沈降性が
良い場合でも上澄水質の濁度又は浮遊物質濃度
(SS濃度)が小さいとは限らないことのよう
に、沈降特性と上澄水のSS濃度とは一般に強
い相関関係を有しない。
(1) When SVI is small, that is, even when the sedimentation properties of activated sludge are good, the turbidity or suspended solids concentration (SS concentration) of the supernatant water is not necessarily small. There is generally no strong correlation with concentration.

(2) 従来のSV又はSVI自動測定装置は汚泥の一
部又は全部が測定管内で浮上したか否かをチエ
ツクすることができず、沈降した汚泥のみを計
測していた。
(2) Conventional SV or SVI automatic measuring devices were unable to check whether some or all of the sludge had floated within the measuring tube, and only measured sludge that had settled.

(3) 活性汚泥処理後の処理水(放流水)SSの排
水基準は、例えば終末下水処理場においては70
mg/以下と定められるが、処理水SSのモニ
ターのみでは基準を越えるもその処置ができな
い。
(3) The discharge standard for treated water (effluent) SS after activated sludge treatment is, for example, 70% at a terminal sewage treatment plant.
mg/mg/or less, but it is not possible to take measures to correct the problem by simply monitoring the treated water SS even if it exceeds the standard.

以上の問題点は浄水場における凝集沈殿プロセ
スにも生じる。
The above problems also occur in the coagulation sedimentation process at water treatment plants.

本発明は、上記問題点に鑑みてなされたもの
で、サンプリング方式による活性汚泥の特性解析
及び上澄水濃度の予測制御を可能にした水質監視
制御方法を提供することを目的とする。
The present invention has been made in view of the above problems, and an object of the present invention is to provide a water quality monitoring and control method that enables characteristic analysis of activated sludge and predictive control of supernatant water concentration using a sampling method.

本発明においては、検水の濁度測定と、この測
定装置による濁度測定結果を解析する演算によつ
て実現される。
The present invention is realized by measuring the turbidity of sample water and calculating the results of the turbidity measurement by this measuring device.

第1図はサンプリングした検水の濁度測定装置
の構造を示す。処理施設よりエアリフト又は水中
ポンプによりサンプリングされた検水は測定管1
に導入される。測定管1の底部には検水中に気泡
を発生させるための曝気装置2が設けられ、検水
のサンプリング完了後一定時間だけ測定管1内検
水を空気かく拌して均一に調整し、濁度測定の準
備処理をなす。光透過式や光反射式で濁度を受光
量変化として測定する濁度計3は測定管1の中央
部より上の部分に設けられ、曝気装置2による検
水の均一調整後のかく拌停止時点から濁度変化測
定を開始する。検水の濁度変化が安定するに必要
な時間(例えば30〜60分)までの測定後、検水は
排水装置4から排水され、必要とする場合には測
定管内壁、底面の洗浄がなされて次回の検水サン
プリングがなされる。この測定サイクルは連続的
に繰り返され、各種水処理制御装置の演算データ
にされる。
Figure 1 shows the structure of a turbidity measuring device for sampled water. Test water sampled from the treatment facility using an airlift or submersible pump is measured in pipe 1.
will be introduced in An aeration device 2 is installed at the bottom of the measuring tube 1 to generate air bubbles in the sample water, and after the sampling of the sample water is completed, the sample water in the measuring tube 1 is agitated with air for a certain period of time to make it uniform and to eliminate turbidity. Prepare for temperature measurement. A turbidity meter 3, which measures turbidity as a change in the amount of received light using a light transmission type or a light reflection type, is installed above the center of the measuring tube 1, and the stirring is stopped after uniformity adjustment of the sample water by the aeration device 2. Start measuring turbidity changes from this point. After measuring for a period of time necessary for the turbidity change of the sample water to stabilize (e.g. 30 to 60 minutes), the sample water is drained from the drainage device 4, and the inner wall and bottom of the measurement tube are cleaned if necessary. The next water sampling will be carried out. This measurement cycle is continuously repeated and used as calculation data for various water treatment control devices.

上記測定装置における沈降測定結果の特性は、
第2図に示すようにa〜dの4つのパターンに大
別される。同図中、特性aは正常に汚泥が沈降す
ることを示し、上澄水の濁度は急速に減少する。
特性bは測定初期の混合液のままの状態(濁度
A)から変化しないことを示し、実際の処理場に
おいても30分汚泥沈降速度SV30が90%以上の場
合も観測される。特性cは汚泥が測定初期から浮
上する場合に見られる現象を示す。特性dは測定
初期の段階では汚泥が一旦沈降するが、測定途中
から汚泥の全部又は一部が浮上したことを示す。
The characteristics of the sedimentation measurement results using the above measuring device are as follows:
As shown in FIG. 2, there are four patterns, a to d. In the figure, characteristic a indicates that sludge settles normally, and the turbidity of supernatant water decreases rapidly.
Characteristic b indicates that there is no change from the mixed liquid state (turbidity A) at the initial stage of measurement, and is observed even in actual treatment plants when the 30-minute sludge settling rate SV 30 is 90% or more. Characteristic c indicates a phenomenon observed when sludge floats from the initial stage of measurement. Characteristic d indicates that the sludge once settles at the initial stage of the measurement, but all or part of the sludge rises to the surface during the measurement.

このように、サンプリング測定装置により測定
管内における汚泥沈降特性を自由沈降に近くし
て、濁度計3による濁度の経時変化を測定する。
これにより、実際の沈殿池の汚泥の複雑な動きと
は異なり、短時間に沈殿池の上澄水濁度又は浮遊
物質濃度の沈降状態(固液分離状態)の経時変化
及び第2図に示す濁度の変化パターンとの比較か
ら汚泥の特性を求めることができ、実際の沈殿池
の滞留時間(2〜4時間程度)に先立つて放流水
の濁度が悪化する前に沈殿池の状態模擬から放流
水(溢流水)濁度を予測して放流水質処理に応用
できる。
In this way, the sludge sedimentation characteristics in the measurement tube are brought close to free sedimentation using the sampling measuring device, and the turbidity meter 3 measures the change in turbidity over time.
As a result, unlike the complicated movement of sludge in an actual sedimentation tank, the turbidity of the supernatant water of the sedimentation tank or the sedimentation state (solid-liquid separation state) of the suspended solids concentration changes over time and the turbidity shown in Figure 2 changes in a short time. The characteristics of the sludge can be determined by comparison with the change pattern, and before the turbidity of the effluent worsens prior to the actual residence time in the settling tank (about 2 to 4 hours), the effluent can be calculated from a simulation of the condition of the settling tank. (Overflow water) Turbidity can be predicted and applied to effluent water quality treatment.

第3図は上記沈殿池の状態予測データを活性汚
泥処理プロセスの水質制御に適用した場合を示
す。処理対象水は曝気槽5に流入して曝気された
後、最終沈殿池6で活性汚泥の沈殿がなされて放
流され、沈殿池6の沈殿活性汚泥は曝気槽5に必
要とされる量だけ返送される。この活性汚泥処理
プロセスにおいて、曝気槽5の入口側又は出口側
もしくは放流口に設けられる薬注装置7から曝気
槽5に凝集剤を注入する高度処理により良好な処
理水質を得る場合、凝集剤の注入率決定に流入負
荷測定装置8による測定値のほかに本発明による
前記サンプリング式濁度測定装置9による放流水
濁度予測値を指標として演算器10が演算決定す
ることで放流水質を早い時期に予測制御して良好
な放流水質制御を可能にする。また。上記高度処
理のほかに、活性汚泥処理水を流入水として凝集
沈殿や塩素注入を行う三次処理に汚泥特性、濁度
の経時変化から予測制御情報を提供することがで
きる。また、浄水場の凝集沈殿池においても活性
汚泥処理の最終沈殿池と同様な機能を有すること
から処理水濁度を予測して混和池への注入率の指
標として利用できる。
FIG. 3 shows a case where the above-mentioned sedimentation tank condition prediction data is applied to water quality control in the activated sludge treatment process. After the water to be treated flows into the aeration tank 5 and is aerated, activated sludge is precipitated in the final settling tank 6 and discharged, and the settled activated sludge in the settling tank 6 is returned to the aeration tank 5 in the required amount. be done. In this activated sludge treatment process, when obtaining good treated water quality through advanced treatment in which a flocculant is injected into the aeration tank 5 from the chemical injection device 7 provided at the inlet or outlet side of the aeration tank 5 or at the outlet, it is necessary to In order to determine the injection rate, in addition to the measured value by the inflow load measuring device 8, the calculation unit 10 calculates and determines the effluent water quality using as an indicator the predicted value of effluent water turbidity obtained by the sampling type turbidity measuring device 9 according to the present invention. predictive control to enable good control of effluent water quality. Also. In addition to the above-mentioned advanced treatment, predictive control information can be provided from sludge characteristics and turbidity changes over time for tertiary treatment, which uses activated sludge treated water as inflow water and performs coagulation sedimentation and chlorine injection. In addition, since the coagulation sedimentation tank in a water treatment plant has the same function as the final sedimentation tank in activated sludge treatment, the turbidity of the treated water can be predicted and used as an index for the injection rate into the mixing tank.

以上のとおり、本発明による沈殿池に対する水
質監視制御方法は、汚泥の沈殿特性及び上澄み液
の濁度(又は浮遊物質濃度)の経時変化を早期に
把握して従来のSV(SVI)計の不十分な計測を補
い、放流水の濁度が悪化する前に状態を予測制御
できるなど良好な水処理を可能にする。
As described above, the water quality monitoring and control method for a sedimentation tank according to the present invention enables the early detection of changes over time in the sedimentation characteristics of sludge and the turbidity (or suspended solids concentration) of the supernatant liquid, thereby preventing the conventional SV (SVI) meter from failing. By supplementing sufficient measurements, it is possible to predict and control the turbidity of effluent water before it worsens, enabling better water treatment.

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

第1図は本発明における濁度測定方法の一実施
例を示す構成図、第2図は処理水の濁度特性図、
第3図は本発明の活性汚泥処理プロセスへの適用
例を示すブロツク図である。 1……測定管、2……曝気装置、3……濁度
計、4……排水装置、5……曝気槽、6……最終
沈殿池、7……薬注装置、8……流入負荷測定装
置、9……濁度測定装置、10……演算器。
FIG. 1 is a configuration diagram showing an example of the turbidity measuring method in the present invention, FIG. 2 is a turbidity characteristic diagram of treated water,
FIG. 3 is a block diagram showing an example of application of the present invention to an activated sludge treatment process. 1... Measuring tube, 2... Aeration device, 3... Turbidity meter, 4... Drainage device, 5... Aeration tank, 6... Final sedimentation tank, 7... Chemical injection device, 8... Inflow load Measuring device, 9...turbidity measuring device, 10... computing unit.

Claims (1)

【特許請求の範囲】[Claims] 1 サンプリングした検水を測定管内で均一濁度
にするに必要な時間だけ空気かく拌し、この空気
かく拌終了時点から該測定管の中央部より上の部
分に固定して設けた濁度計により該検水の濁度の
経時変化を測定し、この経時変化から沈殿池の処
理水の固液分離の状態監視をし、前記経時変化の
パターンから沈殿池の処理水の特性を予測して該
処理水に対する水質処理予測制御を行うことを特
徴とする水質監視制御方法。
1. Air is stirred for the time necessary to make the sampled test water uniform in turbidity in the measuring tube, and from the time the air stirring is finished, a turbidity meter is installed above the center of the measuring tube. The change over time of the turbidity of the sample water is measured, the state of solid-liquid separation of the treated water in the sedimentation tank is monitored from this change over time, and the characteristics of the treated water in the sedimentation tank are predicted from the pattern of the change over time. A water quality monitoring and control method characterized by performing water quality treatment predictive control on the treated water.
JP15532580A 1980-11-05 1980-11-05 Apparatus for monitoring and controlling water quality Granted JPS5778991A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15532580A JPS5778991A (en) 1980-11-05 1980-11-05 Apparatus for monitoring and controlling water quality

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15532580A JPS5778991A (en) 1980-11-05 1980-11-05 Apparatus for monitoring and controlling water quality

Publications (2)

Publication Number Publication Date
JPS5778991A JPS5778991A (en) 1982-05-17
JPH0141111B2 true JPH0141111B2 (en) 1989-09-04

Family

ID=15603417

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15532580A Granted JPS5778991A (en) 1980-11-05 1980-11-05 Apparatus for monitoring and controlling water quality

Country Status (1)

Country Link
JP (1) JPS5778991A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5201372B2 (en) * 2010-05-27 2013-06-05 栗田工業株式会社 Sludge characterization device
WO2020183577A1 (en) * 2019-03-11 2020-09-17 株式会社 ゴーダ水処理技研 Testing method for wastewater treatment facility

Also Published As

Publication number Publication date
JPS5778991A (en) 1982-05-17

Similar Documents

Publication Publication Date Title
US4170553A (en) Process and apparatus for the controlled flocculating or precipitating of foreign substances from a liquid
US5601704A (en) Automatic feedback control system for a water treatment apparatus
CN101306857A (en) Method and device for determining coagulant injection rate in water treatment method
US2154132A (en) Process of controlling the purification of sewage
JP2001137835A (en) Equipment control system
JP3067993B2 (en) Method and apparatus for biological dephosphorization of wastewater
JPH0141111B2 (en)
Mines Jr et al. Conventional and AWT mixed-liquor settling characteristics
JPH02237604A (en) Flocculating and settling device
JPH1099887A (en) Apparatus for controlling addition amount of flocculant
JPH0739000B2 (en) Sludge control device for sedimentation pond
JP3775793B2 (en) Sludge degree measuring method and apparatus
White et al. Experiments on wastewater sedimentation
JPH0415002B2 (en)
JPH0457398B2 (en)
JP2026059523A (en) Water treatment method and water treatment apparatus
JPS5556893A (en) Controlling method for total outgoing sludge of aeration tank in activated sludge method
JPS64118B2 (en)
JPH10192606A (en) How to operate the sand filter tank
JPS58183914A (en) Apparatus for controlling waste sludge of concentration tank
JP2026008756A (en) Sludge volume measuring device and measuring method
KR960000437A (en) Ready-mixed concrete sludge treatment system for manufacturing ready mixed concrete
Reed et al. Sedimentation success from modified jar tests
Wimshurst et al. Enhanced process models for final settlement tanks
JPH04256498A (en) Method and device for controlling water treatment