JP3104764B2 - Excess sludge flow control device - Google Patents
Excess sludge flow control deviceInfo
- Publication number
- JP3104764B2 JP3104764B2 JP03336282A JP33628291A JP3104764B2 JP 3104764 B2 JP3104764 B2 JP 3104764B2 JP 03336282 A JP03336282 A JP 03336282A JP 33628291 A JP33628291 A JP 33628291A JP 3104764 B2 JP3104764 B2 JP 3104764B2
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- flow rate
- sewage treatment
- excess sludge
- flow
- 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
【0001】[0001]
【産業上の利用分野】本発明は、活性汚泥法による下水
処理装置における余剰汚泥流量制御装置に関するもので
ある。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for controlling excess sludge flow in a sewage treatment apparatus using an activated sludge method.
【0002】[0002]
【従来の技術】活性汚泥法による下水処理装置は、図2
に示すように流入下水を最初沈殿池1A、1B、1Cへ
流入させ、沈降性の汚濁物を沈降除去した後、上澄水を
曝気槽2A、2B、2Cに導き、図示しない送風機から
空気を供給しながら、活性汚泥と混合攪拌し、最初沈殿
池上澄水中の汚濁物を活性汚泥に吸着させるとともに、
微生物による酸化分解によって浄化する。最初沈殿池上
澄水と活性汚泥の混合液は、曝気槽から最終沈殿池3
A、3B、3Cに流下させ、最終沈殿池において活性汚
泥と上澄水に沈降分離し、上澄水は滅菌後公共水域へ放
流する。最終沈殿池で沈降した活性汚泥は、返送汚泥ポ
ンプ4A、4B、4Cによって、返送汚泥として曝気槽
へ返送し、循環利用する。また浄化作用によって増量し
た活性汚泥は、余剰汚泥として返送汚泥ラインより余剰
汚泥ポンプ5A、5B、5C及び余剰汚泥流量調整バル
ブ6A、6B、6Cによって引き抜き、余剰汚泥流量計
7A、7B、7Cによって流量を計測しながら、汚泥濃
縮槽8へ投入する。引き抜く余剰汚泥流量の決定につい
ては、種々の方法があるが、図2では曝気槽内の混合液
浮遊物(以下、MLSSという)の濃度を計測するML
SS計9A、9B、9Cの信号と、要求余剰汚泥流量演
算器10A、10B、10Cに予め設定されたMLSS
濃度の目標濃度から引き抜き余剰汚泥量を決定し、余剰
汚泥流量調整装置11A、11B、11Cに出力する方
法を示している。2. Description of the Related Art A sewage treatment apparatus using an activated sludge method is shown in FIG.
As shown in (1), the inflowing sewage is first flowed into the sedimentation basins 1A, 1B, and 1C to settle and remove settling pollutants, and then the supernatant water is guided to the aeration tanks 2A, 2B, and 2C, and air is supplied from a blower (not shown). While mixing with the activated sludge, the sludge in the supernatant water of the sedimentation basin is first adsorbed to the activated sludge,
Purifies by oxidative degradation by microorganisms. The mixed liquid of the first settling tank supernatant water and the activated sludge is supplied from the aeration tank to the final settling tank 3
A, 3B, and 3C, settle and separate into activated sludge and supernatant water in the final sedimentation basin, and the supernatant water is discharged into public waters after sterilization. The activated sludge settled in the final sedimentation basin is returned to the aeration tank as return sludge by the return sludge pumps 4A, 4B, and 4C, and is recycled. The activated sludge increased by the purifying action is extracted as excess sludge from the returned sludge line by the excess sludge pumps 5A, 5B, 5C and the excess sludge flow control valves 6A, 6B, 6C, and the excess sludge is flowed by the excess sludge flow meters 7A, 7B, 7C. Is charged into the sludge thickening tank 8 while measuring. There are various methods for determining the amount of excess sludge to be withdrawn. In FIG. 2, the ML for measuring the concentration of the suspended liquid mixture (hereinafter referred to as MLSS) in the aeration tank is used.
The signals of the SS meters 9A, 9B, 9C and the MLSS preset in the required excess sludge flow rate calculators 10A, 10B, 10C
A method is shown in which the amount of excess sludge to be extracted is determined from the target concentration of the concentration and is output to the excess sludge flow control devices 11A, 11B, 11C.
【0003】[0003]
【発明が解決しようとする課題】上述の活性汚泥法によ
る下水処理装置は、通常は図2に示したように複数の処
理系列を備えており、一つの下水処理系列の最終沈殿池
から余剰汚泥を流通する配管路が、他の下水処理系列の
余剰汚泥の配管路に結合され、最終的には1本の配管路
に集約されて汚泥濃縮槽8に結ばれている。配管路の管
路長、屈折部の有無など下水処理系列ごとに差異があ
り、このため大量の余剰汚泥を引き抜く必要がある場合
には、余剰汚泥の引き抜きが十分に行なえる下水処理系
列とそうでない系列が生ずる。その結果下水処理系列ご
とに保有する活性汚泥量に大きな差が生じ、曝気槽への
送風量や活性汚泥の系内滞留時間の個別管理など下水処
理装置の運転における煩雑さが増大するという欠点があ
った。そこで、本発明では複数の下水処理系列における
余剰汚泥の引き抜き量を均質に保ち、下水処理装置の運
転の簡便性を実現することを目的とする。The sewage treatment apparatus based on the activated sludge method described above usually has a plurality of treatment lines as shown in FIG. 2, and the excess sludge is discharged from the final sedimentation pond of one sewage treatment line. Is connected to the excess sludge pipe line of the other sewage treatment system, and is finally collected into one pipe line and connected to the sludge concentration tank 8. There is a difference between each sewage treatment line, such as the length of the pipe line and the presence or absence of a bent section.If it is necessary to withdraw a large amount of excess sludge, use a sewage treatment line that can sufficiently extract excess sludge. Not occur. As a result, the amount of activated sludge retained by each sewage treatment line varies greatly, and the disadvantage of increasing the complexity of operating the sewage treatment equipment, such as the amount of air blown to the aeration tank and the individual management of the activated sludge residence time in the system, increases. there were. In view of the above, an object of the present invention is to keep the amount of excess sludge withdrawn in a plurality of sewage treatment lines uniform and to realize the simplicity of operation of the sewage treatment device.
【0004】[0004]
【課題を解決するための手段】活性汚泥法による下水処
理系列を複数系列有し、それぞれの下水処理系列からの
余剰汚泥を一つの配管に集約し、濃縮槽へ移送するよう
にした下水処理装置において、曝気槽のMLSS濃度一
定制御アルゴリズムなどを使用して各下水処理系列ごと
に必要な余剰汚泥流量を演算する要求余剰汚泥流量演算
器と、各余剰汚泥引き抜き管路に設けた余剰汚泥流量計
と、要求余剰汚泥流量と実測流量の比率を演算する実測
流量比率演算器と、実測流量比率演算器の出力より、各
下水処理系列の実測流量比率が略同一になるように制御
信号を出力する実測流量比率調整器と、実測流量比率調
整器の出力にしたがって余剰汚泥流量の調節を行なう余
剰汚泥流量調整装置とを設け、各下水処理系の最終沈殿
池からの余剰汚泥流量を要求余剰汚泥流量と実測汚泥流
量の比率が同じになるように制御するようにしている。A sewage treatment apparatus having a plurality of sewage treatment lines by the activated sludge method, wherein excess sludge from each sewage treatment line is collected in one pipe and transferred to a concentration tank. Calculating the required excess sludge flow rate for each sewage treatment system using the MLSS concentration constant control algorithm of the aeration tank, etc., and a surplus sludge flow meter provided in each excess sludge extraction pipe And a control signal for calculating the ratio of the required excess sludge flow rate to the measured flow rate, and a control signal such that the measured flow rate ratio of each sewage treatment system is substantially the same from the output of the measured flow rate calculator. Provided with a measured flow rate regulator and an excess sludge flow control device that adjusts the excess sludge flow according to the output of the measured flow rate regulator, the excess sludge from the final sedimentation basin of each sewage treatment system The ratio of the amount and the required excess sludge flow measured sludge flow rate so as to control to be the same.
【0005】[0005]
【作用】複数の下水処理系列から引き抜く余剰汚泥量の
必要量に対する到達比率を略同じにできるので、複数の
下水処理系列の状態を均質にでき、下水処理装置の運転
を簡便にすることができる。According to the present invention, the arrival ratio of the amount of excess sludge extracted from a plurality of sewage treatment lines to the required amount can be made substantially the same, so that the states of the plurality of sewage treatment lines can be made uniform and the operation of the sewage treatment device can be simplified. .
【0006】[0006]
【実施例】図1は本発明の実施例を示すもので、図2と
同一のものには同一符合を付して詳細な説明を省略す
る。図中12A、12B、12Cは実測流量比率演算
器、13は実測流量比率調整器、14は流量調整動作の
必要性を判定するために予め設定しておく基準実測流量
比率設定器、15は流量調整動作の継続時間を監視する
調整動作継続時間監視装置、16は要求余剰汚泥流演算
装置の出力が前回の出力と比較して小さくなったか否か
を判定する要求余剰汚泥流量監視装置である。次に動作
について説明する。実測流量比率演算器12A、12
B、12Cでは、要求余剰汚泥流量演算器10A、10
B、10Cの出力に対する余剰汚泥流量計7A、7B、
7Cの出力(実測流量)の比率を(1)、(2)、
(3)式によって、演算し、実測流量比率調整器13に
出力する。 aA =QMA /QDA (1) aB =QMB /QDB (2) aC =QMC /QDC (3) ここで、QMA 、QMB 、QMC は余剰汚泥流量計7
A、7B、7Cの出力であり、QDA 、QDB 、QDC
は要求余剰汚泥流量演算器10A、10B、10Cの出
力であり、aA 、aB 、aC は実測流量比率演算器12
A、12B、12Cからの出力である。実測流量比率調
整器13は、前記実測流量比率演算器12A,12B,
12Cの演算比率と基準実測流量比率設定器14に予め
設定した基準実測流量比率aREF と比較し、全ての実測
流量比率aA ,aB ,aC が基準実測流量比率aREF よ
りも高ければ、要求余剰汚泥流量QDA 、QDB 、QD
C を修正することなく、余剰汚泥流量調整装置11A、
11B、11Cに出力する。次に、基準実測流量比率a
REF よりも低い実測流量比率の系列が存在した場合につ
いて説明する。いま下水処理系列Aの実測流量比率aA
が最も小さく、かつ基準実測流量比率aREF よりも低い
場合、下水処理系列B及びCの要求余剰汚泥流量Q
DB 、QDC について修正を加える。修正は(4)、
(5)を用い、全ての下水処理系列の実測流量比率が最
も小さい実測流量比率aA と同じになるよう、修正要求
余剰汚泥流量QDCを演算する。 QDCB =QMB /aA (4) QDCC =QMC /aA (5) (4)、(5)式によって演算された修正要求余剰汚泥
流量を余剰汚泥流量調整装置11B、11Cに出力す
る。このような修正動作を行うと管路を流れる余剰汚泥
量は減少し、修正を行わなかった処理系列Aの実測余剰
汚泥流量QMAは増大し、実測流量比率aA も大きくな
る。大きくなったaA を(4)、(5)式に代入し、再
度修正動作を行う。このようにして複数系列の余剰汚泥
流量の均一性を保ちながら、可及的最大流量を実現する
ことができる。このような要求余剰汚泥流量修正による
調整動作の終了は、調整動作開始時に始動させた調整動
作継続時間監視装置15より設定時間経過後に出力され
る停止指令、あるいは要求余剰汚泥流量が減少した時に
要求余剰汚泥流量監視装置16から出力される停止指令
によって行われる。実施例では、要求余剰汚泥流量の演
算にMLSS一定制御アルゴリズムを使用することにし
たが、流入下水流量に対する比率、あるいは活性汚泥が
系内に滞留する日数(汚泥日令)などを指標として演算
する方法によってもよい。また余剰汚泥流量の調整は流
量調節バルブによって行うことにしたが、余剰汚泥ポン
プの回転数を制御することによって調整するようにして
もよい。FIG. 1 shows an embodiment of the present invention. The same components as those in FIG. 2 are denoted by the same reference numerals, and detailed description is omitted. In the figure, 12A, 12B, and 12C are measured flow rate calculators, 13 is a measured flow rate adjuster, 14 is a reference measured flow rate setter that is set in advance to determine the necessity of the flow rate adjustment operation, and 15 is a flow rate An adjustment operation duration monitoring device 16 for monitoring the duration of the adjustment operation is a required excess sludge flow rate monitoring device that determines whether the output of the required excess sludge flow calculation device has become smaller than the previous output. Next, the operation will be described. Measured flow ratio calculators 12A, 12
In B and 12C, the required excess sludge flow rate calculators 10A and 10A
Excess sludge flow meter 7A, 7B for output of B, 10C,
The ratio of the output (actually measured flow rate) of 7C is (1), (2),
The calculation is performed by the equation (3), and the calculated value is output to the measured flow rate ratio adjuster 13. a A = QM A / QD A (1) a B = QM B / QD B (2) a C = QM C / QD C (3) Here, QM A , QM B , and QM C are surplus sludge flow meters 7.
A, 7B, 7C is the output of, QD A, QD B, QD C
A request excess sludge flow calculator 10A, 10B, 10C output, a A, a B, a C is measured flow ratio calculator 12
Outputs from A, 12B, and 12C. The measured flow ratio adjuster 13 includes the measured flow ratio calculators 12A and 12B,
The calculated ratio of 12C is compared with the reference measured flow ratio a REF preset in the reference measured flow ratio setting device 14, and if all the measured flow ratios a A , a B , and a C are higher than the reference measured flow ratio a REF. , required excess sludge flow rate QD A, QD B, QD
Without modifying C , the excess sludge flow control device 11A,
Output to 11B and 11C. Next, the reference measured flow rate a
A case where a series of the measured flow rate ratio lower than REF exists will be described. Now the measured flow rate a A of the sewage treatment system A
Is smaller than the reference measured flow ratio a REF , the required excess sludge flow Q of the sewage treatment systems B and C is
D B, make modifications for QD C. Correction is (4),
(5) using, so that the actual flow rate ratio of all the sewage processing sequence is the same as the smallest measured flow ratio a A, calculates the modification request excess sludge flow QDC. QDC B = QM B / a A (4) QDC C = QM C / a A (5) (4), (5) outputs a correction request excess sludge flow rate calculated by the equation excess sludge flow controller 11B, and 11C I do. Such Doing corrective action excess sludge amount flowing through pipeline decreases, measured excess sludge flow rate QM A of do not fix processing sequence A is increased, the greater the measured flow ratio a A. Largely became a A (4), by substituting in (5), take corrective action again. In this way, the maximum possible flow rate can be realized while maintaining the uniformity of the excess sludge flow rates of a plurality of systems. The end of the adjusting operation by such a correction of the required excess sludge flow rate is determined by a stop command output after a lapse of a set time from the adjusting operation continuation time monitoring device 15 started at the start of the adjusting operation, or requested when the required excess sludge flow rate decreases. This is performed by a stop command output from the surplus sludge flow monitoring device 16. In the embodiment, the MLSS constant control algorithm is used to calculate the required excess sludge flow rate, but the calculation is performed using the ratio to the inflow sewage flow rate or the number of days (sludge age) in which activated sludge stays in the system as an index. Depending on the method. Although the adjustment of the excess sludge flow rate is performed by the flow rate control valve, the adjustment may be performed by controlling the number of rotations of the excess sludge pump.
【0006】[0006]
【発明の効果】本発明は上述のように、各下水処理系列
の要求余剰汚泥流量に対する実測の余剰汚泥流量の比率
が同一となり、各下水処理系列を略同一の状態に保つこ
とができるので、複数の下水処理系列からなる下水処理
装置の運転を簡便にすることができる。As described above, according to the present invention, the ratio of the measured excess sludge flow rate to the required excess sludge flow rate of each sewage treatment line becomes the same, and each sewage treatment line can be maintained in substantially the same state. The operation of the sewage treatment apparatus including a plurality of sewage treatment systems can be simplified.
【図1】本発明の実施例を示す余剰汚泥流量制御装置の
ブロック図FIG. 1 is a block diagram of a surplus sludge flow control device showing an embodiment of the present invention.
【図2】従来の余剰汚泥流量制御装置のブロック図FIG. 2 is a block diagram of a conventional excess sludge flow control device.
1A、1B、1C 最初沈殿池 2A、2B、2C 曝気槽 3A、3B、3C 最終沈殿池 4A、4B、4C 返送汚泥ポンプ 5A、5B、5C 余剰汚泥ポンプ 6A、6B、6C 余剰汚泥流量調節バルブ 7A、7B、7C 余剰汚泥流量計 8 汚泥濃縮槽 9A、9B、9C MLSS計 10A、10B、10C 要求余剰汚泥流量演算器 11A、11B、11C 余剰汚泥流量調整装置 12A、12B、12C 実測流量比率演算器 13 実測流量比率調整器 14 基準実測流量比率 15 調整動作継続時間監視装置 16A、16B、16C 要求余剰汚泥流量監視装置 1A, 1B, 1C First settling tank 2A, 2B, 2C Aeration tank 3A, 3B, 3C Final settling tank 4A, 4B, 4C Return sludge pump 5A, 5B, 5C Excess sludge pump 6A, 6B, 6C Excess sludge flow control valve 7A , 7B, 7C Surplus sludge flow meter 8 Sludge concentration tank 9A, 9B, 9C MLSS meter 10A, 10B, 10C Required surplus sludge flow calculator 11A, 11B, 11C Excess sludge flow controller 12A, 12B, 12C Actual measurement flow ratio calculator 13 Measured flow ratio adjuster 14 Reference measured flow ratio 15 Adjustment operation duration monitoring device 16A, 16B, 16C Required surplus sludge flow monitoring device
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平5−138187(JP,A) 特開 昭60−175597(JP,A) 特開 昭59−109290(JP,A) 特開 昭59−59293(JP,A) (58)調査した分野(Int.Cl.7,DB名) C02F 3/12 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-5-138187 (JP, A) JP-A-60-175597 (JP, A) JP-A-59-109290 (JP, A) JP-A-59-109290 59293 (JP, A) (58) Field surveyed (Int. Cl. 7 , DB name) C02F 3/12
Claims (1)
列有し、それぞれの下水処理系列からの余剰汚泥を一つ
の配管に集約し、濃縮槽へ移送するようにした下水処理
装置において、曝気槽のMLSS制御アルゴリズムなど
を使用して各下水処理系列ごとに必要な余剰汚泥流量を
演算する要求余剰汚泥流量演算器と、各余剰汚泥引き抜
き管路に設けた余剰汚泥流量計と、要求余剰汚泥流量と
実測流量の比率を演算する実測流量比率演算器と、各実
測流量比率演算器の出力を入力し、各下水処理系列の実
測流量比率が略同一になるように演算する実測流量比率
調整器と、実測流量比率調整器の出力にしたがって余剰
汚泥流量の調節を行なう余剰汚泥流量調整装置とを設
け、各下水処理系の最終沈殿池からの余剰汚泥流量を要
求余剰汚泥流量と実測汚泥流量の比率が同じになるよう
に制御することを特徴とする余剰汚泥流量制御装置。1. A sewage treatment apparatus comprising a plurality of sewage treatment lines by the activated sludge method, wherein excess sludge from each sewage treatment line is collected in one pipe and transferred to a concentration tank. Required sludge flow calculator for calculating the required excess sludge flow for each sewage treatment system using the MLSS control algorithm, etc., a surplus sludge flow meter provided in each surplus sludge extraction pipe, and a required surplus sludge flow And a measured flow rate calculator that calculates the ratio of the measured flow rate, and an output of each measured flow rate calculator that calculates the measured flow rate ratio of each sewage treatment system so that the measured flow rate ratios are approximately the same. A surplus sludge flow control device that adjusts the surplus sludge flow according to the output of the measured flow rate ratio controller, and measures the surplus sludge flow from the final sedimentation basin of each sewage treatment system with the required surplus sludge flow An excess sludge flow control device, wherein the sludge flow ratio is controlled to be the same.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP03336282A JP3104764B2 (en) | 1991-11-25 | 1991-11-25 | Excess sludge flow control device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP03336282A JP3104764B2 (en) | 1991-11-25 | 1991-11-25 | Excess sludge flow control device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH05138188A JPH05138188A (en) | 1993-06-01 |
| JP3104764B2 true JP3104764B2 (en) | 2000-10-30 |
Family
ID=18297502
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP03336282A Expired - Fee Related JP3104764B2 (en) | 1991-11-25 | 1991-11-25 | Excess sludge flow control device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3104764B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6359489B2 (en) * | 2015-06-12 | 2018-07-18 | 水ing株式会社 | Sewage treatment method and sewage treatment system |
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1991
- 1991-11-25 JP JP03336282A patent/JP3104764B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH05138188A (en) | 1993-06-01 |
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