JPS5916596A - Removal device for excess sludge - Google Patents

Removal device for excess sludge

Info

Publication number
JPS5916596A
JPS5916596A JP57122950A JP12295082A JPS5916596A JP S5916596 A JPS5916596 A JP S5916596A JP 57122950 A JP57122950 A JP 57122950A JP 12295082 A JP12295082 A JP 12295082A JP S5916596 A JPS5916596 A JP S5916596A
Authority
JP
Japan
Prior art keywords
sludge
return
pump
basin
surplus
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
JP57122950A
Other languages
Japanese (ja)
Inventor
Mitsuo Oku
奥 満男
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
Tokyo Shibaura Electric 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 Toshiba Corp, Tokyo Shibaura Electric Co Ltd filed Critical Toshiba Corp
Priority to JP57122950A priority Critical patent/JPS5916596A/en
Publication of JPS5916596A publication Critical patent/JPS5916596A/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 make the amt. of the sludge to be accumulated in each basin uniform, by determining the deviation value of the flow rate of the return sludge from each basin from the flow rate of the return sludge to be returned with a return sludge pump from the respective basin of a final settling basin and removing the excess sludge in accordance with the results thereof. CONSTITUTION:The activated sludge scraped by a sludge scraper 3 in, for example, four sludge accumulating inlets 2 in a settling basin 1 is returned by a return sludge pump 4 into an aeration tank, and the flow rates of the return sludge removed from the inlets 2 are measured with electromagnetic flowmeters 5 for return sludge. The excess sludge is branched from the removal pipings of the respective sludge accumulating inlets and is removed through electrically driven selector valves 6 provided for each of the basins by means of an excess sludge pump 7. The removal flow rate of the excess sludge in this stage is measured with an electromagnetic flowmeter 8 for the excess sludge. When a removal command is emitted to an excess removal command 9 in such constitution, the command is inputted to a calculator 10.

Description

【発明の詳細な説明】 〔発明の技術分野〕 活性汚泥法による水処理設備において最終沈殿池に滞積
した余剰汚泥を引抜く余剰汚泥引抜装置に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to an excess sludge extraction device for extracting excess sludge accumulated in a final settling tank in a water treatment facility using an activated sludge method.

〔技術的背景〕[Technical background]

通常最終沈殿池は2つ以上の複数の池九区分され各池に
は汚泥掻寄機によシ1個所の汚泥集積桝へ掻寄せ留めら
れる。
Normally, the final settling tank is divided into nine sections, each consisting of two or more ponds, and each pond has a sludge scraping machine that scrapes the sludge into one sludge collection basin.

返送汚泥ポンプは各汚泥集積桝に対し共通で設備され汚
泥集積桝よシ汚泥を引抜きその総流量が予じめ設定され
た返送汚泥目標量に合うべき、連続的な運転制御がなさ
れるのが一般的である。
The return sludge pump is commonly installed for each sludge accumulation basin, and its operation is continuously controlled so that the total flow rate of the sludge drawn out from the sludge accumulation basin should match a preset return sludge target amount. Common.

一方余剰汚泥引抜きポンプの運転はタイムスケジューヤ
による定量引抜きであシ、これも各汚泥集積材に対し共
通の設備とされる事から各汚泥集積材よシの一斉引き抜
きを行い予じめ設定された目標総引抜量に相当するまで
引抜いて終了する間欠運転である。
On the other hand, the operation of the surplus sludge removal pump is by quantitative drawing using a time scheduler, and since this equipment is common to each sludge accumulation material, it is set in advance to pull out all sludge accumulation materials at the same time. This is an intermittent operation that ends when the target total withdrawal amount is reached.

従来返送汚泥ポンプの運転は前記の如く総返送汚泥流量
であシ各池毎の引抜き偏差量は問題としていなかった。
Conventionally, the return sludge pump was operated based on the total return sludge flow rate as described above, and the drawing deviation amount for each pond was not considered a problem.

しかしこの運転によれば、例えば設備系にょシ各池引抜
汚泥集積桝から返送汚泥ポンプまでの配管抵抗損失はポ
ンプ配置と6池の汚泥果績桝引抜点までの配管長、構造
から必然的に決定され、その損失量は各汚泥集積桝毎に
一様ではない。この結果、連続的に返送汚泥ポンプにょ
シ引抜かれる各池毎の返送引抜量に偏差が生じ、−等、
損失の高い池の汚泥引抜き量が一等少なくな9、余剰と
して蓄積され結果的には汚泥フロックとして最終沈殿池
よシ越流し汚泥流出する事につながる問題がある。
However, according to this operation, for example, the piping resistance loss from the sludge collection basin for each pond to the return sludge pump will inevitably occur due to the pump arrangement, the length and structure of the piping to the sludge output point of the six ponds, and the structure. The amount of loss is not uniform for each sludge collection basin. As a result, deviations occur in the amount of return sludge drawn from each pond that is continuously drawn by the return sludge pump, etc.
The amount of sludge extracted from ponds with high losses is extremely low (9), which leads to the accumulation of surplus sludge, which eventually leads to sludge flowing out of the final settling tank as sludge flocs.

〔発明の概要〕[Summary of the invention]

本発明は複数の池に区分きれ活性汚泥によシ水処理する
沈殿池と、これらの各沈殿池に設けられ汚泥を集積する
汚泥集積材と、沈殿池に設置され汚泥集積材に汚泥を掻
寄せる汚泥掻寄イ幾と、汚泥集積材に掻寄せられた汚泥
を曝気槽に送シ返えす返送汚泥ポンプと、汚泥集積材に
集積された汚泥で曝気槽に返送する必要のない余剰の汚
泥を引抜く余剰汚泥ポンプと、この余剰汚泥ポンプに一
端を接続され他端を汚泥集積材又は汚泥集積材から引出
きれた配管に接続された余剰汚泥引抜用の電動切換弁と
、余剰汚泥ポンプの配信系に接続され引抜かれた余剰汚
泥の流量全計則する゛α磁流量計と、電動切換弁の開閉
制御及び余剰汚泥ポンプの運転制御を行う制御装置とか
らなる余剰汚泥引抜装置に於て、一端を汚泥集積材に他
端を返送汚泥ポンプに接続され引抜かれる返送汚泥の流
量を計測する返送汚泥電磁流量計と、これらの返送汚泥
電磁流量計によって計測された返送汚泥流量の偏差値を
演算し余剰汚泥ポンプによシ引抜く余剰汚泥引抜量を制
御装置に出力する演算器とを備えた余剰汚泥引抜装置で
ある。
The present invention consists of a sedimentation tank divided into a plurality of ponds for treating water with activated sludge, a sludge accumulating material installed in each of these settling basins for accumulating sludge, and a sludge accumulating material installed in the settling basin to scrape sludge into the sludge accumulating material. A sludge scraper that collects sludge, a return sludge pump that sends the sludge collected on the sludge accumulating material back to the aeration tank, and a sludge collected on the sludge accumulating material that does not need to be returned to the aeration tank. an electric switching valve for removing surplus sludge, which has one end connected to the surplus sludge pump and the other end connected to a sludge accumulating material or a pipe that has been pulled out from the sludge accumulating material; In the surplus sludge extraction equipment, which consists of an α magnetic flowmeter connected to the distribution system and which measures the total flow rate of the extracted surplus sludge, and a control device that controls the opening and closing of the electric switching valve and the operation of the surplus sludge pump. , a return sludge electromagnetic flowmeter that measures the flow rate of the returned sludge that is connected to the sludge accumulation material at one end and a return sludge pump at the other end, and the deviation value of the return sludge flow rate measured by these return sludge electromagnetic flowmeters. This surplus sludge extraction device is equipped with a computing unit that calculates and outputs the amount of surplus sludge to be extracted by the surplus sludge pump to a control device.

即ち本発明は最終沈殿池の6池から返送汚泥ポンプによ
り返送される返送汚泥流■゛から6池の返送汚泥流量の
偏差t’に求め、この結果より余剰汚泥ポンプによシ引
抜く余剰汚泥引抜量を決定して行く余剰汚泥引抜装置で
ある。
That is, the present invention calculates the deviation t' of the return sludge flow rate of the 6 ponds from the return sludge flow returned by the return sludge pump from the 6 final settling tanks, and from this result, the surplus sludge that is extracted by the surplus sludge pump. This is an excess sludge extraction device that determines the amount of sludge to be extracted.

本発明は前記のように構成したので6池の返送汚泥引抜
きによる引抜流量の偏差分として蓄積した汚泥を平均化
した余剰汚泥引抜制御をとる事が出来、余剰汚泥が汚泥
フロックとして最終沈殿池よシ越流し汚泥流出するとい
う事がないという効果を生ずる。
Since the present invention is configured as described above, it is possible to perform excess sludge extraction control that averages the sludge accumulated as a deviation of the withdrawal flow rate due to return sludge withdrawal from the six ponds, and the surplus sludge is transferred to the final settling tank as sludge flocs. This has the effect of preventing sludge from flowing out overflow.

〔発明の実施例〕[Embodiments of the invention]

次に本発明の詳細な説明する。図面は複数の池に区分さ
れ活性汚泥によシ水処理する沈殿池Jと、沈殿池1に設
けられ汚泥を集積する汚泥集積材2と、沈殿池1に設置
され汚泥集積材2に汚泥を掻寄せる汚泥掻寄機3と、汚
泥集積材2に掻寄せられた汚泥を曝気槽に送り返えす返
送汚泥ポンプ4と、汚泥集積材2に集積された汚泥で曝
気槽に返送する必要のない余剰の汚泥を引抜く余剰汚泥
ポンプ7と、余剰汚泥ポンプ7に一端を接続され他端を
汚泥集積材2又は汚泥集積材2から引出された配管2a
に接続された余剰汚泥引抜用の電動切換弁6と、余剰汚
泥ポンプ7の配管系に接続され引抜かれた余剰汚泥の流
量を計測する電磁流量計8と、電動切換弁6の開閉制御
及び余剰汚泥ポンプ7の運転制御を行う制御装置11.
13とからなる余剰汚泥引抜装置に於て、一端を汚泥集
積材2に他端を返送汚泥ポンプ4に接続され引抜かれる
返送汚泥の流量を計測する返送汚泥電磁流量計5と、返
送汚泥電磁流量計5によって計測された返送汚泥流量の
偏差値を演算し余剰汚泥ポンプ7によシ引抜く余剰汚泥
引抜量を制御装置11に出力する演算器10とを備えた
余剰汚泥引抜装置を示している。
Next, the present invention will be explained in detail. The drawing shows a sedimentation tank J that is divided into multiple ponds and processes water using activated sludge, a sludge accumulation material 2 installed in the sedimentation tank 1 that collects sludge, and a sludge accumulation material 2 installed in the sedimentation tank 1 that collects sludge. A sludge scraper 3 that collects sludge, a return sludge pump 4 that sends the sludge collected on the sludge accumulating material 2 back to the aeration tank, and the sludge accumulated on the sludge accumulating material 2 does not need to be returned to the aeration tank. A surplus sludge pump 7 that pulls out surplus sludge, and a pipe 2a whose one end is connected to the surplus sludge pump 7 and whose other end is drawn out from the sludge accumulating material 2 or the sludge accumulating material 2.
An electromagnetic flow meter 8 connected to the piping system of the surplus sludge pump 7 for measuring the flow rate of the extracted surplus sludge, and an electric switching valve 6 for controlling the opening and closing of the electric switching valve 6 and for controlling the surplus sludge. A control device 11 that controls the operation of the sludge pump 7.
13, a return sludge electromagnetic flow meter 5 which is connected to the sludge accumulating material 2 at one end and the return sludge pump 4 at the other end and measures the flow rate of the return sludge to be drawn; and a return sludge electromagnetic flow rate meter 5. 5 shows an excess sludge extraction device equipped with a calculator 10 that calculates the deviation value of the return sludge flow rate measured by the total 5 and outputs the amount of excess sludge extracted by the excess sludge pump 7 to the control device 11. .

沈殿池1において例えば四池の汚泥集積桝2に汚泥掻寄
機3によシ、掻寄せられた活性汚泥は返送汚泥ポンプ4
によシ曝気溝へ返送される各々の汚泥集積桝2よシ引抜
かれた返送汚泥訃は返送汚泥1に磁流置針5によシ計測
される。
In the settling tank 1, for example, activated sludge is sent to the sludge collection basins 2 of four ponds by the sludge scraper 3, and the collected activated sludge is sent to the return sludge pump 4.
The amount of returned sludge drawn out from each sludge collection basin 2 to be returned to the aeration groove is measured by a magnetic flow pointer 5 in the returned sludge 1.

一方余剰汚泥は各汚泥集積桝の引抜き配管よ多分岐され
各地銀に設けた電動切換弁6余通して余剰汚泥ポンプ7
によシ引抜かれる。この時余剰汚泥引抜流量は余剰汚泥
電磁流量計8によシ計測される。
On the other hand, excess sludge is transferred to multiple branches from the extraction piping of each sludge collection basin, passed through the electric switching valve 6 installed in each bank, and then passed through the excess sludge pump 7.
It is pulled out. At this time, the surplus sludge extraction flow rate is measured by the surplus sludge electromagnetic flow meter 8.

この様な構成において、余剰引抜き指令9により引抜き
指令が出されると演算器】0へ入力される。
In such a configuration, when a withdrawal command is issued by the surplus withdrawal command 9, it is input to the arithmetic unit 0.

演算器10には前回引抜き指令から今回引抜き指令まで
の各地銀返送汚泥流瀘全各々入カレ積算しておき、この
値と予じめ設定された余剰汚泥引抜き総目標流量ΣQs
とによシ各池より余剰汚泥として引抜く池面の余剰汚泥
引抜流量目標値ΔQsを演算して制iI器11へ与える
。制御器11では余A4磁流量計8により計測された余
剰汚泥引抜と地銀の余剰汚泥引抜流量目標値とが一致し
た時点で制御信号12ヲシーケンス制御器13へ入力す
る7−ケンス制御器13ではこの指令によシ仄の池引抜
きへ移行させるべく前記余剰汚泥引抜き電動切換弁6を
切換て行き最終性引抜きまで同様に行い最終地終沈と同
じに余剰汚泥ポンプは停止し切換弁が全閉となシ次の余
剰汚泥引抜きIji4始指令が出るまで待機する。
The calculation unit 10 integrates the total amount of sludge returned to each bank from the previous extraction command to the current extraction command, and combines this value with the preset surplus sludge extraction total target flow rate ΣQs.
A target value ΔQs of the flow rate of excess sludge on the pond surface to be extracted as excess sludge from each pond is calculated and given to the controller 11. The controller 11 inputs a control signal 12 to the sequence controller 13 when the excess sludge extraction measured by the A4 magnetic flow meter 8 matches the target value of the surplus sludge extraction flow rate of the local bank. Based on this command, the electric switching valve 6 for excess sludge removal is switched to shift to the secondary pond extraction, and the same process is carried out until the final extraction, and the excess sludge pump is stopped and the switching valve is fully closed. Tonanashi waits until the next surplus sludge removal Iji 4 start command is issued.

演算器10では下記演算を行う。The calculator 10 performs the following calculations.

± 値 Qs:余剰汚泥引抜流量目標値 QRI :第1池よシの返送汚泥流蓋積算値(前回余剰
引抜指令) Q旧:第2池よシの返送汚泥流量積算値(〜今回余剰引
抜指令までのm詳) Qim:第3池よシの返送汚泥流量積算値QR4二第4
池よりの返送汚泥流量積算値即ち6池返送量の積算結果
から返送量の偏差値が得られるので、その逆数比例値を
予じめ設定された余剰汚泥引抜流量目標値に乗じた値を
求める拳によシー等返送鈑の多い池の割合の汁だけ一等
返送讐の少ない池から余剰引抜きをする事様な各池余剰
汚泥引抜流量目標値を求める。
± value Qs: Surplus sludge withdrawal flow rate target value QRI: Return sludge flow cap integrated value for the 1st pond (previous surplus withdrawal command) Q old: Accumulated return sludge flow rate for the 2nd pond (~current surplus withdrawal command) m details) Qim: Integrated value of return sludge flow rate from No.3 pond QR42 No.4
Since the deviation value of the return amount can be obtained from the integrated value of the return sludge flow rate from the ponds, that is, the integrated result of the return amount of the six ponds, the value obtained by multiplying the reciprocal proportional value by the preset excess sludge withdrawal flow rate target value is calculated. A target value of the flow rate for excess sludge removal from each pond is determined, such that a proportion of the excess sludge from ponds with a large number of returned sludges is removed from ponds with few returned sludges.

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

図面は本発明の一実施例金示す説明図である。 1・・・沈殿池 2・・・汚泥集積桝 3・・・汚泥掻寄機 4・・・返送汚泥ポンプ 5・・・返送汚泥′9L磁流量計 6・・・余剰汚泥引抜電動切換弁 7・・・余剰汚泥ポンプ 8・・・余剰汚泥電磁流量計 10・・・演算器 11・・・制御器 13・・・シーケンス制御器 The drawings are explanatory diagrams showing one embodiment of the present invention. 1... Sedimentation pond 2...Sludge collection basin 3...Sludge scraping machine 4...Return sludge pump 5...Return sludge '9L magnetic flowmeter 6...Excess sludge removal electric switching valve 7... Surplus sludge pump 8... Surplus sludge electromagnetic flowmeter 10... Arithmetic unit 11...Controller 13...Sequence controller

Claims (1)

【特許請求の範囲】[Claims] 複数の池に区分され活性汚泥によシ水処理する沈殿池と
、これらの各沈殿池に設けられ汚泥を集積する汚泥集積
桝と、前記沈殿池に設置され前記汚泥集積桝に汚泥を掻
寄せる汚泥掻寄機と、前記汚泥集積桝に掻寄せられた汚
泥を曝気槽に送シ返えす返送汚泥ポンプと、前記汚泥集
積桝に集積された汚泥で前記曝気槽に返送する必要のな
い余剰の汚泥を引抜く余剰汚泥ポンプと、この余剰汚泥
ポンプに一端を接続され他端を前記汚泥集積桝又は汚泥
集穣桝から引出された配管に接続でれた余剰汚泥引抜用
の電動切換弁と、前記余剰汚泥ポンプの配管系に接続さ
れ引抜かれた余剰汚泥の流量を計測する電磁流量計と、
前記+ji、動切倶弁の開閉制御及び前記余剰汚泥ポン
プの運転制菌ヲ行う制御装置とからなる余剰汚泥引抜装
置に於て、一端全前記汚泥呆積桝に他端を前記返送汚泥
ポンプに接続され引抜かれる返送汚泥の流量全計測する
返送汚泥電磁流量計と、これらの返送汚泥電磁流量計に
よって計測された返送汚泥流量の偏差値を演算し前記余
剰汚泥ポンプによシ引抜く余剰汚泥引抜量を前記制御装
置に出力する演算器とを備えた余剰汚泥引抜装置。
A sedimentation basin divided into a plurality of ponds for treating water with activated sludge, a sludge collection basin installed in each of these sedimentation basins for accumulating sludge, and a sludge accumulation basin installed in the sedimentation basin for collecting sludge into the sludge accumulation basin. A sludge scraping machine, a return sludge pump that sends the sludge collected in the sludge accumulation basin back to the aeration tank, and a sludge collecting machine that collects surplus sludge that does not need to be returned to the aeration tank. an excess sludge pump for extracting sludge; an electric switching valve for extracting excess sludge, one end of which is connected to the excess sludge pump and the other end connected to the sludge collection basin or a pipe drawn out from the sludge collection basin; an electromagnetic flowmeter connected to the piping system of the surplus sludge pump and measuring the flow rate of the extracted surplus sludge;
In the surplus sludge extraction device comprising a control device for controlling the opening/closing of the movable shut-off valve and controlling the operation of the surplus sludge pump, one end is connected to the sludge storage tank and the other end is connected to the return sludge pump. A return sludge electromagnetic flowmeter that is connected and measures the total flow rate of the return sludge to be drawn out, and a deviation value of the return sludge flow rate measured by these return sludge electromagnetic flowmeters is calculated and extracted by the surplus sludge pump. An apparatus for extracting excess sludge, comprising a computing unit that outputs the amount to the control device.
JP57122950A 1982-07-16 1982-07-16 Removal device for excess sludge Pending JPS5916596A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57122950A JPS5916596A (en) 1982-07-16 1982-07-16 Removal device for excess sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57122950A JPS5916596A (en) 1982-07-16 1982-07-16 Removal device for excess sludge

Publications (1)

Publication Number Publication Date
JPS5916596A true JPS5916596A (en) 1984-01-27

Family

ID=14848628

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57122950A Pending JPS5916596A (en) 1982-07-16 1982-07-16 Removal device for excess sludge

Country Status (1)

Country Link
JP (1) JPS5916596A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61183397A (en) * 1985-02-09 1986-08-16 デグツサ・アクチエンゲゼルシヤフト Granular builder
JPS6270220A (en) * 1985-08-23 1987-03-31 Zenji Hagiwara Amorphous aluminosilicate filler and method for producing the same

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61183397A (en) * 1985-02-09 1986-08-16 デグツサ・アクチエンゲゼルシヤフト Granular builder
JPS6270220A (en) * 1985-08-23 1987-03-31 Zenji Hagiwara Amorphous aluminosilicate filler and method for producing the same

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