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JPS587326B2 - How to manage sludge volume at sewage treatment plants - Google Patents
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JPS587326B2 - How to manage sludge volume at sewage treatment plants - Google Patents

How to manage sludge volume at sewage treatment plants

Info

Publication number
JPS587326B2
JPS587326B2 JP50051133A JP5113375A JPS587326B2 JP S587326 B2 JPS587326 B2 JP S587326B2 JP 50051133 A JP50051133 A JP 50051133A JP 5113375 A JP5113375 A JP 5113375A JP S587326 B2 JPS587326 B2 JP S587326B2
Authority
JP
Japan
Prior art keywords
sludge
concentration
amount
sewage treatment
volume
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
JP50051133A
Other languages
Japanese (ja)
Other versions
JPS51125967A (en
Inventor
逸朗 藤田
宏成 高林
茂 吉田
英幸 林
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.)
Yaskawa Electric Corp
Original Assignee
Yaskawa 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 Yaskawa Electric Manufacturing Co Ltd filed Critical Yaskawa Electric Manufacturing Co Ltd
Priority to JP50051133A priority Critical patent/JPS587326B2/en
Publication of JPS51125967A publication Critical patent/JPS51125967A/en
Publication of JPS587326B2 publication Critical patent/JPS587326B2/en
Expired 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)

Description

【発明の詳細な説明】 本発明は、下水処理場において、沈澱池内に堆積した汚
泥量を、汚泥濃度分布を計測することによって連続的に
正確に測定する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for continuously and accurately measuring the amount of sludge deposited in a settling tank in a sewage treatment plant by measuring the sludge concentration distribution.

下水処理において、最初沈澱池、最終沈澱池ま,たは汚
泥濃縮槽に堆積している汚泥の量を正確に把握すること
は、下水処理の全プロセスを効率よく運転するために重
要である。
In sewage treatment, it is important to accurately grasp the amount of sludge deposited in the initial settling tank, final settling tank, or sludge thickening tank in order to operate the entire sewage treatment process efficiently.

原水に浮遊物を含まない有機性廃水を、活性汚泥法によ
り処理するとき、いわゆる食物−微生物比(F−M比)
を一定の範囲内たとえば下水処理では0.2〜0.5に
保持しないと、処理が不十分になったり、汚泥の沈降状
態が悪くなることが知られている。
When treating organic wastewater that does not contain suspended matter in the raw water using the activated sludge method, the so-called food-microbe ratio (F-M ratio)
It is known that if the value is not maintained within a certain range, for example, 0.2 to 0.5 in sewage treatment, the treatment will be insufficient and the state of sludge sedimentation will deteriorate.

F−M比を一定にするために(生成汚泥量)/(汚泥量
)を一定にする方法があり、それには汚泥量の計測が必
要となる。
In order to keep the FM ratio constant, there is a method of keeping (amount of generated sludge)/(amount of sludge) constant, and this requires measurement of the amount of sludge.

ところで、汚泥量は曝気槽内活性汚泥量と最終沈澱池内
汚泥量の和であり、曝気槽内活性汚泥量は、濃度計によ
り濃度を求めて槽容積を乗算すればよいが、最終沈澱池
内の汚泥量測定法としては、従来、光学的あるいはその
他の方法で、沈澱池内に堆積した汚泥の界面を検出して
汚泥容積を求め、これに返送汚泥濃度を乗算して汚泥量
を求める方法がある。
By the way, the amount of sludge is the sum of the amount of activated sludge in the aeration tank and the amount of sludge in the final settling tank, and the amount of activated sludge in the aeration tank can be determined by finding the concentration using a densitometer and multiplying it by the tank volume. Conventional methods for measuring the amount of sludge include detecting the interface of the sludge accumulated in the sedimentation tank using optical or other methods to determine the sludge volume, and then multiplying this by the concentration of returned sludge to determine the amount of sludge. .

しかし、汚泥界面高さが同じでも、汚泥の固形物量には
かなり差のある場合があり、このような方法では、実際
の汚泥量との誤差が大きく、余剰汚泥の排泥量およびそ
の系内にとどめておくべき汚泥量の管理が困難であった
However, even if the sludge interface height is the same, there may be a considerable difference in the amount of solids in the sludge, and with this method, there is a large error between the actual amount of sludge and the amount of excess sludge discharged and the amount inside the system. It was difficult to manage the amount of sludge that should be kept at a minimum.

また、最初沈澱池、汚泥濃縮槽においても、汚泥量の管
理が必要であり、各沈澱池での滞留時間は沈澱池内汚泥
量に比例するので、滞留時間の制御のためにも堆積汚泥
量の測定が必要である。
In addition, it is necessary to control the amount of sludge in the initial sedimentation tank and sludge thickening tank, and the residence time in each sedimentation tank is proportional to the amount of sludge in the sedimentation tank. Measurement is required.

本発明は、上述の点にかんがみ、沈澱池内の汚泥量を正
確に測定しようとするもので、沈澱池内で汚泥に浸漬さ
れる濃度検出器と、その検出出力を増幅する増幅器を組
み合わせて浸漬形の汚泥濃度計を構成し、沈澱池の汚泥
内に浸漬した濃度検出器を上下動駆動装置によって上下
動させ、沈澱池内の汚泥濃度分布を計測して汚泥量を算
出するようにしたものである。
In view of the above-mentioned points, the present invention aims to accurately measure the amount of sludge in a sedimentation tank, and uses a combination of a concentration detector that is immersed in sludge in the sedimentation tank and an amplifier that amplifies its detection output. The sludge concentration meter consists of a concentration detector immersed in the sludge in the settling tank, which is moved up and down by a vertical movement drive device to measure the sludge concentration distribution in the settling tank and calculate the amount of sludge. .

すなわち、沈澱池の構造から深さ方向の各部の寸法が明
らかであるから、汚泥界面以下を深さ方向の微小部分に
わけ、各部分の体積とその深さの濃度を乗算して、その
総和を求めれば堆積汚泥量を計算することができる。
In other words, since the dimensions of each part in the depth direction are clear from the structure of the sedimentation tank, the area below the sludge interface is divided into minute parts in the depth direction, the volume of each part is multiplied by the concentration at that depth, and the total sum is calculated. The amount of accumulated sludge can be calculated by finding .

この方法によれば沈澱池内の汚泥の量、堆積状態、濃度
分布、界面の変動が適確に把握できるので、沈澱池の運
転管理に役立つばかりでなく、汚泥滞留時間(Soli
deRetention Time)制御や汚泥回転数
(Numberof Sludge Revoluti
on)制御などの制御方法を実際に適用するうえで有効
な手段となり得る。
With this method, the amount of sludge in the sedimentation tank, the state of its accumulation, the concentration distribution, and the fluctuations in the interface can be accurately grasped, so it is not only useful for the operation management of the sedimentation tank, but also the sludge retention time (Solid
DeRetention Time) control and sludge rotation speed (Number of Sludge Revolution)
It can be an effective means for actually applying control methods such as on) control.

第1図は本発明の下水道処理における最終沈澱池の概略
を示す側面図で、1は流入管、2は整流板、3は排泥管
、4は汚泥ホツパー、5は液面、6は汚泥界面、7はか
きよせ機のチェーン、8はかきよせ機駆動装置、9はア
イドラ、10は超音波による濃度検出器、11は吊持ケ
ーブル、12は検出器上下動装置である。
Figure 1 is a side view schematically showing the final settling tank in the sewage treatment of the present invention, where 1 is an inflow pipe, 2 is a rectifier plate, 3 is a sludge pipe, 4 is a sludge hopper, 5 is a liquid level, and 6 is a sludge tank. 7 is a scraper chain, 8 is a scraper drive device, 9 is an idler, 10 is an ultrasonic concentration detector, 11 is a suspension cable, and 12 is a detector vertical movement device.

沈澱池上部に設置した検出器上下動装置により吊持ケー
ブル11で濃度検出器10を上下動させ、深さに対応し
て超音波の減衰量をXYレコーダに連続記録させる。
The concentration detector 10 is moved up and down with a suspension cable 11 by a detector vertical movement device installed at the upper part of the sedimentation tank, and the amount of attenuation of the ultrasonic waves is continuously recorded on an XY recorder in accordance with the depth.

濃度検出器10が上限または下限に達したら、タイマに
よる一定時間の休止のあと、XYレコーダのチャートを
自動的に新しい面に進め、濃度検出器の移動方向を逆に
する。
When the concentration detector 10 reaches the upper or lower limit, the chart of the XY recorder is automatically advanced to a new surface and the direction of movement of the concentration detector is reversed after a pause for a certain period of time by a timer.

測定周期は、濃度検出器の上下動のための所要時間以上
であれば、休止時間の調整により任意に設定でき、深さ
方向に分割設定した各区分ごとにその深さに対応する濃
度と体積を乗算し、その総和により汚泥量を求める。
The measurement period can be set arbitrarily by adjusting the pause time as long as it is longer than the time required for the vertical movement of the concentration detector. The amount of sludge is calculated by multiplying by the total amount.

第2図は、本発明によって測定した最終沈澱池の深さ方
向の濃度分布測定記録例で、汚泥ホッパー4の深さ3m
、汚泥ホツパーの底から液面5までの深さ6.5mで3
時間ごとに濃度検出器を上昇および下降させている。
Figure 2 shows an example of the concentration distribution measurement record in the depth direction of the final sedimentation basin measured according to the present invention, where the sludge hopper 4 was measured at a depth of 3 m.
, 3 at a depth of 6.5 m from the bottom of the sludge hopper to the liquid level 5.
The concentration detector is raised and lowered every hour.

この結果、一般に汚泥界面6より深いところでは、深く
なるほど汚泥濃度が高くなっているが、場合によっては
、第2図Aで示されるように途中に低濃度または高濃度
の層が存在することがあり、また、下水道システムにお
ける返送汚泥の濃度は、測定の結果、ホツパーの底の部
分の濃度とほぼ一致しており、堆積汚泥の平均濃度より
も高いことがわかった。
As a result, the sludge concentration generally increases deeper than the sludge interface 6, but in some cases there may be a layer of low or high concentration in the middle, as shown in Figure 2A. Furthermore, the concentration of returned sludge in the sewerage system was found to be approximately the same as the concentration at the bottom of the hopper, and higher than the average concentration of accumulated sludge.

したがって、従来のように汚泥体積と返送汚泥濃度の積
から汚泥量を求める方法は、汚泥濃度の分布状態や、平
均濃度の点からも、かなりの誤差を生じるものであるこ
とが明らかとなった。
Therefore, it has become clear that the conventional method of calculating sludge volume from the product of sludge volume and returned sludge concentration causes a considerable error in terms of the distribution of sludge concentration and the average concentration. .

第3図は本発明による汚泥濃度測定例の一部を詳細に示
したもので、縦軸d〔m〕はホツパー底面からの高さを
示し、曲線3A,3Bは同じ個所の異なる測定日時にお
ける濃度分布曲線である。
Figure 3 shows in detail a part of an example of sludge concentration measurement according to the present invention, where the vertical axis d [m] indicates the height from the bottom of the hopper, and curves 3A and 3B show the same point at different measurement dates and times. This is a concentration distribution curve.

濃度分布曲線3A,3Bから汚泥界面の高さはそれぞれ
2.25m,2.1mでほぼ一致している。
From the concentration distribution curves 3A and 3B, the heights of the sludge interface are 2.25 m and 2.1 m, respectively, which are almost the same.

また、3A,3Bの曲線を高さ0に外挿して堆積汚泥の
最も底の部分の濃度を求めると、それぞれ7kg/m3
,4kg/m3となる。
Furthermore, when we extrapolate the curves 3A and 3B to a height of 0 to find the concentration at the bottom of the accumulated sludge, the concentration is 7 kg/m3, respectively.
, 4kg/m3.

経験上、返送汚泥の濃度は底の部分の濃度とほぼ等しい
と考えられるので、従来の方法では、この返送汚泥濃度
に界面高さから算出した汚泥体積を乗算して汚泥量を算
出しているが、本発明の測定により、曲線3A,3Bか
ら明らかなように、汚泥濃度は全体が一様でなく、深さ
によって変化しており、返送汚泥濃度が汚泥ホツパー内
の実際の濃度を示すものではなく、また日時により濃度
の分布状態が著るしく異なることが判明し、従来の方法
で算出する汚泥量は、実際の汚泥量と大きな差があるこ
とがわかった。
From experience, the concentration of returned sludge is considered to be approximately equal to the concentration at the bottom, so in the conventional method, the sludge volume is calculated by multiplying the returned sludge concentration by the sludge volume calculated from the interface height. However, as is clear from curves 3A and 3B, the measurement of the present invention shows that the sludge concentration is not uniform throughout and changes depending on the depth, and the returned sludge concentration indicates the actual concentration in the sludge hopper. However, it was also found that the concentration distribution state differed significantly depending on the date and time, and it was found that the amount of sludge calculated using the conventional method differed greatly from the actual amount of sludge.

本発明は、汚泥濃度検出器を堆積汚泥中に浸漬して上下
動させながら、汚泥ホツパー内の汚泥濃度分布を計測し
、汚泥界面以下を深さ方向の微小体積に分割して、各分
割部分ごとに濃度と体積を乗算し、その総和を求めるよ
うにしてあるので、実際の汚泥量を正確に計量できると
ともに、汚泥の濃度分布が明らかとなり、汚泥量の管理
を有効に行ない得る効果がある。
The present invention measures the sludge concentration distribution in the sludge hopper by immersing the sludge concentration detector into the accumulated sludge and moving it up and down, and divides the area below the sludge interface into minute volumes in the depth direction. Since the concentration and volume are multiplied for each volume and the sum is determined, the actual sludge volume can be measured accurately, and the concentration distribution of sludge becomes clear, which has the effect of effectively managing the sludge volume. .

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

第1図は本発明が実施される沈澱池構造の概略を示す側
断面図、第2図は本発明による濃度分布測定結果の例を
示すグラフ、第3図は測定例の一部の詳細図である。 1は流入管、2は整流板、3は排泥管、4は汚泥ホツパ
ー、5は液面、6は汚泥界面、7はかきよせ機のチェー
ン、8はかきよせ機駆動装置、9はアイドラ、10は濃
度検出器、11は吊持ケーブル、12は検出器上下動装
置である。
FIG. 1 is a side sectional view showing an outline of the sedimentation tank structure in which the present invention is implemented, FIG. 2 is a graph showing an example of concentration distribution measurement results according to the present invention, and FIG. 3 is a detailed view of a part of the measurement example. It is. 1 is an inflow pipe, 2 is a current plate, 3 is a sludge drain pipe, 4 is a sludge hopper, 5 is a liquid level, 6 is a sludge interface, 7 is a chain of the scraper, 8 is a scraper drive device, 9 is an idler , 10 is a concentration detector, 11 is a suspension cable, and 12 is a detector vertical movement device.

Claims (1)

【特許請求の範囲】[Claims] 1 汚泥濃度稜出器を汚泥中に浸漬して上下動させ、汚
泥ホッパー内の深さ方向に連続した汚泥濃度分布を計測
し、汚泥界面以下の深さ方向に分割した微小部分ごとに
計測した濃度と体積を乗算し、その総和により汚泥量を
検出することを特徴とする下水処理場の汚泥量管理方法
1. A sludge concentration extractor was immersed in sludge and moved up and down to measure the continuous sludge concentration distribution in the depth direction within the sludge hopper, and measurements were taken for each minute portion divided in the depth direction below the sludge interface. A method for controlling the amount of sludge in a sewage treatment plant, which is characterized by multiplying concentration and volume and detecting the amount of sludge by the sum of the two.
JP50051133A 1975-04-24 1975-04-24 How to manage sludge volume at sewage treatment plants Expired JPS587326B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP50051133A JPS587326B2 (en) 1975-04-24 1975-04-24 How to manage sludge volume at sewage treatment plants

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP50051133A JPS587326B2 (en) 1975-04-24 1975-04-24 How to manage sludge volume at sewage treatment plants

Publications (2)

Publication Number Publication Date
JPS51125967A JPS51125967A (en) 1976-11-02
JPS587326B2 true JPS587326B2 (en) 1983-02-09

Family

ID=12878307

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50051133A Expired JPS587326B2 (en) 1975-04-24 1975-04-24 How to manage sludge volume at sewage treatment plants

Country Status (1)

Country Link
JP (1) JPS587326B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57107293A (en) * 1980-12-26 1982-07-03 Meidensha Electric Mfg Co Ltd Method for controlling amount of activated sludge
JPS6014993A (en) * 1983-07-04 1985-01-25 Nishihara Environ Sanit Res Corp Batch treating apparatus for activated sludge

Also Published As

Publication number Publication date
JPS51125967A (en) 1976-11-02

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