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JPH0471596B2 - - Google Patents
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JPH0471596B2 - - Google Patents

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Publication number
JPH0471596B2
JPH0471596B2 JP62300408A JP30040887A JPH0471596B2 JP H0471596 B2 JPH0471596 B2 JP H0471596B2 JP 62300408 A JP62300408 A JP 62300408A JP 30040887 A JP30040887 A JP 30040887A JP H0471596 B2 JPH0471596 B2 JP H0471596B2
Authority
JP
Japan
Prior art keywords
filtration
water
flow rate
basin
ponds
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
JP62300408A
Other languages
Japanese (ja)
Other versions
JPH01143678A (en
Inventor
Yasuyuki Myajima
Takatoshi Kato
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
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 Tokyo Shibaura Electric Co Ltd filed Critical Tokyo Shibaura Electric Co Ltd
Priority to JP62300408A priority Critical patent/JPH01143678A/en
Publication of JPH01143678A publication Critical patent/JPH01143678A/en
Publication of JPH0471596B2 publication Critical patent/JPH0471596B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 [発明の目的] (産業上の利用分野) 本発明は、ろ過池の池数を制御する浄水場のろ
過池数制御装置に係わり、特に浄水場の水処理流
量に応じて適正な数のろ過池を稼働させて各ろ過
池のろ床の保護を図る浄水場のろ過池数制御装置
に関する。
[Detailed Description of the Invention] [Object of the Invention] (Industrial Application Field) The present invention relates to a filter number control device for a water treatment plant that controls the number of filters, and particularly to a water treatment plant flow rate. The present invention relates to a device for controlling the number of filters in a water purification plant, which operates an appropriate number of filters to protect the filter beds of each filter.

(従来の技術) 一般に、浄水場の水処理行程は、取水ポンプで
取込んだ原水を着水井に着水させた後沈でん池に
導き、ここで原水に含まれる混濁物質や浮遊物等
を薬注処理により沈でん分離し、そのとき得られ
る上澄水を沈でん池流出渠を経てろ過池に導いて
ろ過した後、更に必要に応じて浄水池、配水池等
を通して一般需要家へ送水される。
(Prior art) Generally, in the water treatment process at a water purification plant, raw water is taken in by a water intake pump, lands in a landing well, and then is guided to a settling pond, where the turbid substances and suspended matter contained in the raw water are removed by medicines. Sedimentation is separated by injection treatment, and the resulting supernatant water is led to a filtration pond via a sedimentation basin outflow conduit, where it is filtered, and then, if necessary, water is sent to general consumers through a water purification pond, a water distribution pond, etc.

ところで、以上のような浄水場では、通常、沈
でん池流出渠からの上澄水は複数のをろ過池でろ
過され、かつ、それらろ過池には個別にろ過流量
調節弁が設けられ、浄水場の水処理流量に応じて
各ろ過池のろ過流量調節弁の開度を調整しながら
ろ過全体のろ過流量(以下、総ろ過流量と呼ぶ)
を得ている。しかし、ろ過洗浄効率等の面から考
えた場合、各ろ過池の運転は予め定めたろ過流量
設定範囲内でろ過流量を得るのが望ましい。この
場合、何らかの事故で浄水場の水処理流量が大幅
に変化したとき、各ろ過池が設定範囲内でろ過流
量を得るための運転を行うことは非常に難しく、
その水処理流量に応じてろ過池の池数を増減させ
ながら運転を行う必要がある。
By the way, in the above-mentioned water treatment plants, the supernatant water from the sedimentation basin outflow drain is usually filtered through multiple filtration basins, and each of these filtration basins is individually equipped with a filtration flow rate control valve. The filtration flow rate of the entire filtration (hereinafter referred to as the total filtration flow rate) is adjusted by adjusting the opening degree of the filtration flow rate control valve of each filtration basin according to the water treatment flow rate.
I am getting . However, in terms of filtration cleaning efficiency, etc., it is desirable to operate each filter to obtain a filtration flow rate within a predetermined filtration flow rate setting range. In this case, when the water treatment flow rate at the water treatment plant changes significantly due to some kind of accident, it is extremely difficult to operate each filtration basin to obtain the filtration flow rate within the set range.
It is necessary to operate the filter while increasing or decreasing the number of filters depending on the water treatment flow rate.

従来、以上のように水処理流量が大幅に変化し
た場合、人手によりろ過池の流入弁および流出弁
等を開閉操作しろ過池の池数を増減させている。
しかし、例えば取水ポンプのトリツプ事故のよう
に水処理流量が急激に減少したとき、人手による
ろ過池の休止作業は長時間に及ぶために適正な運
転を継続させることは困難である。このことは取
水ポンプが復電し水処理流量が急激に回復した場
合にも同様のことが言える。
Conventionally, when the water treatment flow rate changes significantly as described above, the number of filters is increased or decreased by manually opening and closing the inlet and outlet valves of the filters.
However, when the water treatment flow rate suddenly decreases, as in the case of a water intake pump trip accident, for example, it is difficult to maintain proper operation because it takes a long time to manually shut down the filtration basin. The same thing can be said when the power is restored to the water intake pump and the water treatment flow rate suddenly recovers.

(発明が解決しようとする問題点) 従つて、以上のような浄水場においては、水処
理流量が急激に変化したとき、人手による介入で
は適切な処置を講じることが難しく、ろ過池の水
位の低下によつて当該ろ過池のろ床が空気中に露
出するといつた2次故障を引起こす問題がある。
すなわち、ろ過池のろ床が空気中に露出してろ床
砂層に空気が入つた後そのろ過池を再生する場
合、ろ過池に徐々に水を張りながらろ床内の空気
を追出し、ろ床を洗浄し本来のろ過能力に戻す必
要がある。この水を張る作業は一般に現場で人手
により弁を操作しながら行うので、一度ろ床に空
気が入つてしまうと再び稼働させるには相当な時
間を必要とし、かつ、その間ろ過可能なろ過池数
が不足となつているので取水ポンプが復電しても
水を処理することができず浄水場の機能を停止せ
ざるを得ないといつた問題がある。また、復電に
より取水ポンプを再起動させた場合、ポンプには
最低吐出流量が定められているので、着水流量の
急激な増加が起こる。その結果、浄水場の着水流
量が急激に増加したとき、それに伴つてろ過流量
を増加させないと沈でん池流出渠の水位は急激に
上昇し、沈でん池がオーバフローするといつた事
態が発生する。
(Problem to be Solved by the Invention) Therefore, in the above-mentioned water treatment plants, when the water treatment flow rate changes suddenly, it is difficult to take appropriate measures with manual intervention, and the water level of the filtration basin may be There is a problem in that the filter bed of the filtration basin is exposed to the air due to the drop, causing secondary failure.
In other words, when regenerating the filter bed after the filter bed of the filter bed is exposed to the air and air enters the sand layer of the filter bed, the air inside the filter bed is expelled while gradually filling the filter bed with water. It needs to be cleaned and restored to its original filtration capacity. This work of filling water is generally done on-site by manipulating valves, so once air gets into the filter bed, it takes a considerable amount of time to restart the operation, and the number of filters that can filter during that time is The problem is that even if the water intake pumps are restored to power, they will not be able to process the water and the water treatment plant will have to stop functioning. Furthermore, when the water intake pump is restarted due to power restoration, the pump has a minimum discharge flow rate, so the water landing flow rate increases rapidly. As a result, when the flow rate of water arriving at the water treatment plant increases rapidly, unless the filtration flow rate is increased accordingly, the water level in the sedimentation basin outflow channel will rise rapidly, causing a situation where the sedimentation basin will overflow.

本発明は以上のような問題点を解決するために
なされたもので、浄水場プロセスのトータル的な
観点から異常状態を検出して稼働すべきろ過池を
自動的に増減し、これによつてろ過池の水位の低
下を防いでろ過池のろ床の露出を未然に回避し、
かつ、沈でん池流出渠の水位異常高によるオーバ
ーフローを防止し、浄水場の安定な運転を確保す
る浄水場のろ過池数制御装置を提供することを目
的とする。
The present invention was made to solve the above-mentioned problems, and detects abnormal conditions from a total perspective of the water treatment plant process and automatically increases or decreases the number of filters to be operated. Preventing the water level of the filtration basin from dropping and preventing exposure of the filtration basin's bed.
Another object of the present invention is to provide a filter number control device for a water purification plant that prevents overflow due to an abnormally high water level in a sedimentation basin outflow conduit and ensures stable operation of the water purification plant.

[発明の構成] (問題点を解決するための手段) 本発明による浄水場のろ過池数制御装置は、取
水ポンプで取り込んだ原水に含まれる混濁物質、
浮遊物等を、着水井、沈でん池、沈でん池流出渠
および複数のろ過池を通して沈でん、ろ過等によ
る水処理を行い、その水処理流量に応じて稼働す
るろ過池の池数を増減制御する浄水場のろ過池数
制御装置において、前記沈でん池流出渠を含む前
処理段階でプロセス状態信号を取得するプロセス
状態信号取得手段と、このプロセス状態信号取得
手段で取得された浄水場プロセスの異常状態を検
出する異常検出手段と、この異常検出手段から異
常検出信号を受けたとき、観測時間内での前記沈
殿でん池流出渠の水位変化量から制御タイミング
時間を求めた後、この制御タイミング時間に基づ
いて起動または停止するろ過池の池数を決定し、
この池数に基づいて起動または停止するろ過池を
決定するろ過池数決定手段とを設けたものであ
る。
[Structure of the Invention] (Means for Solving the Problems) The device for controlling the number of filtration ponds in a water purification plant according to the present invention is capable of controlling turbid substances contained in raw water taken in by a water intake pump,
Water treatment that processes floating matter through settling, filtration, etc. through an incoming well, settling basin, settling basin outflow channel, and multiple filtration basins, and controlling the number of filtration basins in operation according to the water treatment flow rate. In the field filtration tank number control device, a process state signal acquisition means for acquiring a process state signal at a pretreatment stage including the sedimentation basin outflow conduit, and an abnormal state of the water purification plant process acquired by the process state signal acquisition means are provided. When an abnormality detection signal is received from the abnormality detection means to be detected and the abnormality detection signal is received from the abnormality detection means, the control timing time is determined from the amount of water level change in the sedimentation basin outflow culvert within the observation time, and then the control timing time is Determine the number of filters to start or stop based on
A number-of-filtration determining means is provided for determining which filter to start or stop based on this number of filters.

(作用) 従つて、本発明は、以上のような手段とするこ
とにより、プロセス状態信号取得手段で取得した
プロセス状態信号と予め定めた設定値とに基づい
て前期異常検出手段が浄水場プロセスの種々の観
点から異常の有無を調べ、異常である判断したと
きに制御タイミング時間を求めた後、このタイミ
ング時間に基づいて起動または停止するろ過池の
池数を決定し、この池数に基づいて起動または停
止するろ過池を順次決定し、該当するろ過池を起
動または停止していくものである。
(Function) Therefore, in the present invention, by using the above means, the abnormality detection means detects the water purification plant process based on the process state signal acquired by the process state signal acquisition means and the predetermined setting value. After examining the presence or absence of an abnormality from various viewpoints and determining the control timing time when it is determined that there is an abnormality, the number of filters to be started or stopped is determined based on this timing time, and the number of filters to be started or stopped is determined based on this timing time. The filtration basins to be started or stopped are determined in sequence, and the corresponding filtration basins are started or stopped.

(実施例) 以下、本発明の実施例について図面を参照して
説明する。第1図は本発明装置の一実施例を示す
全体構成図であつて、この装置を大きく分けると
浄水場10とろ過池数制御装置20とで構成され
ている。
(Example) Hereinafter, an example of the present invention will be described with reference to the drawings. FIG. 1 is an overall configuration diagram showing one embodiment of the device of the present invention, and this device is roughly divided into a water purification plant 10 and a filter number control device 20.

前記浄水場10は、従来周知の如く原水11を
取水ポンプ12,…で取り込んだ後、着水井1
3、沈でん池14、沈でん池流出渠15、複数の
ろ過池16,…および浄水池17等を通過させな
がら原水中に含む混濁物質や浮遊物等を除去し、
かつ、ろ過洗浄した後送水ポンプ18を用いて需
要家へ送水する一連の水浄化作用を行う施設であ
る。なお、沈でん池14と沈でん池流出渠15と
の間には所定高さの沈でん池流出堰が設けられ、
沈でん池14の流量が沈でん池流出堰を越流して
沈でん流出渠15に送られる。
As is well known in the art, the water purification plant 10 takes in raw water 11 with water pumps 12, . . .
3. Remove turbid substances, suspended matter, etc. contained in the raw water while passing through the sedimentation basin 14, sedimentation basin outflow drain 15, multiple filtration basins 16, ... and water purification basin 17, etc.,
It is also a facility that performs a series of water purification operations, such as filtering and cleaning and then sending water to consumers using a water pump 18. In addition, a sedimentation pond outflow weir of a predetermined height is provided between the sedimentation pond 14 and the sedimentation pond outflow culvert 15,
The flow rate of the sedimentation basin 14 overflows the sedimentation basin outflow weir and is sent to the sedimentation basin outflow culvert 15.

一方、前記ろ過池数制御装置20には、対象プ
ロセスの状態信号を取得するプロセス状態信号取
得手段が設けられている。このプロセス状態信号
取得手段は、所望とする箇所に取得目的に応じた
検出器を設けて対象プロセスの運転状態を判断す
るためのプロセス状態信号を取得するものであ
り、具体的には例えば取水ポンプ12の運転台数
S1、着水井13の着水流量値S2(または沈で
ん池14の沈でん池総流入流量値S3)、沈でん
池流出渠15の沈でん池流出渠水位S4等が取得
される。
On the other hand, the filter number control device 20 is provided with process status signal acquisition means for acquiring status signals of the target process. This process status signal acquisition means acquires a process status signal for determining the operating status of the target process by installing a detector according to the acquisition purpose at a desired location, and specifically, for example, a water intake pump. 12 operating units S1, the landing flow rate value S2 of the landing well 13 (or the sedimentation basin total inflow flow rate value S3 of the sedimentation basin 14), the sedimentation basin outflow conduit water level S4 of the sedimentation basin outflow conduit 15, etc. are acquired.

また、前記ろ過池数制御装置20には前記各信
号S1〜S4から対象プロセスの異常状態を検出
する異常検出手段が設けられている。この異常検
出手段は、取水ポンプ運転台数S1と取水ポンプ
運転台数設定値S1′とを比較し取水ポンプ運転
台数の異常を検出する取水ポンプ停止検出手段2
1と、着水流量S2または沈でん池総流入流量S
3と流量変化設定値S2′を比較し浄水場のろ過
池16への流入流量が流量変化設定値以上変化し
たときに異常を検出する着水流量異常検出手段2
2と、沈でん池流出渠水位S4と沈でん池流出渠
水位変化設定値S4′とを比較し沈でん池流出渠
の水位が単位時間内に設定値以上変化したときに
異常を検出する水位変化異常検出手段23等によ
つて構成される。なお、これら取水ポンプ停止検
出手段21、着水流量異常検出手段22、水位変
化異常検出手段23はプロセス状態信号S1〜S
4を並行に取込んでそれぞれ異常状態の有無を判
断しているが、最も沈でん池流出渠水位S4がろ
過流量の状態を反映させているので、少なくとも
水位変化異常検出手段23を用いて沈でん池流出
渠水位S4を取得しプロセスの異常状態を判断す
ることが必要である。
Further, the filter number control device 20 is provided with an abnormality detection means for detecting an abnormal state of the target process from each of the signals S1 to S4. This abnormality detection means is a water intake pump stop detection means 2 that compares the number of water intake pumps in operation S1 and a set value S1' for the number of water intake pumps in operation and detects an abnormality in the number of water intake pumps in operation.
1, and the landing flow rate S2 or the total sedimentation pond inflow flow rate S
3 and a flow rate change set value S2', and detects an abnormality when the inflow flow rate to the filtration basin 16 of the water purification plant changes by more than the flow rate change set value.
2, water level change abnormality detection that compares the sedimentation basin outflow conduit water level S4 and the sedimentation basin outflow conduit water level change set value S4' and detects an abnormality when the water level of the sedimentation basin outflow conduit changes by more than the set value within a unit time. It is constituted by means 23 and the like. In addition, these water intake pump stop detection means 21, water landing flow rate abnormality detection means 22, and water level change abnormality detection means 23 process state signals S1 to S.
4 are taken in parallel to determine whether there is an abnormal state, but since the sedimentation basin outflow conduit water level S4 most reflects the state of the filtration flow rate, at least the water level change abnormality detection means 23 is used to detect the sedimentation basin outflow conduit water level S4. It is necessary to obtain the outflow channel water level S4 and determine the abnormal state of the process.

前記取水ポンプ停止検出手段21、着水流量異
常検出手段22および水位変化異常検出手段23
等の出力は制御タイミング決定手段24に送出さ
れる。この制御タイミング決定手段24は各手段
21〜23の何れかの異常検出信号と沈でん池流
出渠水位S4とに基づいて制御タイミングを決定
する機能を持つている。25は制御タイミング決
定手段24から制御タイミング信号を受けて沈で
ん池流出渠水位S4に基づいて起動または停止す
べき池数を決定する起動・停止池数決定手段であ
り、ここで決定された起動または停止池数信号は
起動・停止池決定手段26に導入される。この起
動・停止池決定手段26は起動または停止すべき
池数のほか、各ろ過池16,…の弁開閉状態信号
S11、ろ抗信号S12、ろ過流量S13および
池決定基準設定値S14が入力され、起動または
停止すべきろ過池の池番号および当該池番号のろ
過池16の状態目標値(例えば起動または停止)
を決定し出力する。なお、これらの手段21〜2
6等は後述するが、制御用コンピユータを用いて
ソフト的に処理するかあるいはハードな構成によ
り実現する。
The intake pump stop detection means 21, the water landing flow abnormality detection means 22, and the water level change abnormality detection means 23
These outputs are sent to the control timing determining means 24. The control timing determining means 24 has a function of determining the control timing based on the abnormality detection signal from any one of the means 21 to 23 and the sedimentation pond outflow channel water level S4. Reference numeral 25 denotes a starting/stopping pond number determining means which receives a control timing signal from the control timing determining means 24 and determines the number of ponds to be started or stopped based on the sedimentation pond outflow channel water level S4, and the activated or stopped pond number determined here is The stop pond number signal is introduced into the start/stop pond determining means 26. In addition to the number of ponds to be started or stopped, the start/stop pond determining means 26 receives input of the valve opening/closing state signal S11, filtration signal S12, filtration flow rate S13, and pond determination standard setting value S14 of each filter basin 16,... , the pond number of the filtration basin to be started or stopped, and the state target value of the filtration basin 16 of the relevant pond number (for example, starting or stopping)
Determine and output. In addition, these means 21-2
6, etc., which will be described later, can be realized by software processing using a control computer or by a hardware configuration.

30は操作端制御部であつて、これは起動・停
止池番号決定手段26からの状態目標値に従つて
例えばシーケンス制御によつて該当ろ過池16に
設置されている弁へ開閉指令信号S15を出力し
て調節を行い、ろ過池16の状態を状態目標値と
なる様に制御するものであつて、例えばシーケン
スコントローラを用いて実現する。なお、対象プ
ロセスへの信号入出力はデータ伝送装置を用いて
行う。図中31は流量計、32は水位計である。
Reference numeral 30 denotes an operating end control unit, which sends an open/close command signal S15 to the valve installed in the corresponding filter basin 16 by sequence control, for example, according to the state target value from the start/stop basin number determining means 26. The output is output and adjusted to control the state of the filter 16 to a target state value, and is realized using, for example, a sequence controller. Note that signal input/output to the target process is performed using a data transmission device. In the figure, 31 is a flow meter, and 32 is a water level meter.

次に、以上のように構成された装置の動作を説
明するに先立ち、第2図を用いて浄水場の水位高
低関係から適正なろ過池16の池数を用いて運転
させる必要性について説明する。今、沈でん池流
出渠15の水位hは、浄水場の水処理流量をQ、
ろ過池16のろ過流量をqとすると、 ∂h/∂t=1/A(Q−oi=1 qi) ……(1) なる式に基づいて変化する。但し、nはろ過池1
6の並列数、A(m2)は沈でん池流出渠15の面
積である。従つて、浄水場の水処理流量Qに比
べ、各ろ過池16のろ過流量の総和oi=1 qiが大きい
ときには沈でん池流出渠15の水位hは下降し、
逆に各ろ過池16のろ過流量の総和oi=1 qiが小さい
ときには沈でん池流出渠15の水位hは上昇す
る。また、浄水場の水処理流量Qは沈でん池総流
入流量Q′にほぼ等しく、これは着水流量にほぼ
等しい。従つて、何らかの理由で着水流量が急激
に減少した場合、それに伴つて水処理流量Qおよ
び沈でん池流出渠水位hも急激に低下する。この
沈でん池流出渠水位hが規定値以下に低下する
と、一般にろ過池16のろ床16aの水位が浄水
池17の水位よりも高く作られているので、ろ床
16aが空気に触れてしまう可能性が出てくる。
従つて、水処理流量Qが急激に減少したとき、稼
働中のろ過池数を減少させて沈でん池流出渠水位
hの急激な低下を防ぐ必要がある。なお、ろ床1
6aの砂層に空気が入ると、すべてのろ過池16
に徐々に水を張り、ろ床16a内から空気を追出
さなければろ過能力が回復せず、再び浄水場を稼
働させるには相当な時間を必要とする。
Next, before explaining the operation of the device configured as described above, the necessity of operating the device using an appropriate number of filters 16 based on the water level relationship of the water purification plant will be explained using Fig. 2. . Now, the water level h of the sedimentation basin outflow channel 15 is the water treatment flow rate of the water treatment plant, Q,
When the filtration flow rate of the filtration basin 16 is q, it changes based on the following formula: ∂h/∂t=1/A(Q− oi=1 qi) (1). However, n is filtration pond 1
6 in parallel, A (m 2 ) is the area of the sedimentation basin outflow conduit 15. Therefore, when the sum oi=1 qi of the filtration flow rate of each filtration basin 16 is large compared to the water treatment flow rate Q of the water purification plant, the water level h of the sedimentation basin outflow culvert 15 decreases,
Conversely, when the sum oi=1 qi of the filtration flow rate of each filtration basin 16 is small, the water level h of the sedimentation basin outflow culvert 15 rises. Further, the water treatment flow rate Q of the water treatment plant is approximately equal to the total inflow flow rate Q' of the sedimentation pond, which is approximately equal to the landing flow rate. Therefore, if the landing flow rate suddenly decreases for some reason, the water treatment flow rate Q and the settling basin outflow channel water level h also decrease rapidly. If the water level h of the sedimentation basin outflow channel falls below the specified value, the water level of the filter bed 16a of the filtration basin 16 is generally made higher than the water level of the water purification basin 17, so the filter bed 16a may come into contact with air. Gender comes out.
Therefore, when the water treatment flow rate Q suddenly decreases, it is necessary to reduce the number of filtration ponds in operation to prevent a sudden drop in the sedimentation basin outflow water level h. In addition, filter bed 1
When air enters the sand layer 6a, all the filters 16
The filtration capacity will not be restored unless the air is gradually filled with water and the air is expelled from the filter bed 16a, and it will take a considerable amount of time to restart the water purification plant.

一方、取水ポンプ所の復電などの理由で取水ポ
ンプ12が再起動した場合、ポンプ12には最低
吐出流量が定められているので、それに伴つて着
水流量が増加する。その結果、浄水場の水処理流
量Qも急激に増加する。水処理流量Qが急激に増
加すると沈でん池流出渠15の水位hが急激に増
加し、その結果、沈でん池14はオーバーフロー
する。従つて、水処理流量Qが急激に増加した場
合、ろ過池16の池数を増加して沈でん池流出渠
水位hの急激な増加を防ぐ必要がある。
On the other hand, when the water intake pump 12 is restarted due to power restoration at the water intake pump station, etc., the minimum discharge flow rate is determined for the pump 12, so the landing flow rate increases accordingly. As a result, the water treatment flow rate Q at the water purification plant also increases rapidly. When the water treatment flow rate Q rapidly increases, the water level h of the sedimentation basin outflow conduit 15 increases rapidly, and as a result, the sedimentation basin 14 overflows. Therefore, when the water treatment flow rate Q suddenly increases, it is necessary to increase the number of filtration basins 16 to prevent a sudden increase in the sedimentation basin outflow water level h.

以上のように本装置においては浄水場の水処理
流量に応じて適正な池数のろ過池16を稼働させ
る必要があり、以下、本発明装置の動作について
第3図を参照しながら説明する。電源の投入によ
り本装置の動作が開始すると、ステツプST1に示
すように取水ポンプ停止検出手段21、着水流量
異常検出手段22および水位変化異常検出手段2
3がそれぞれ取水ポンプ運転台数S1、着水流量
S2(または沈でん池総流入流量S3)、沈でん
池流出渠水位S4を取込み、各設定値S1′,S
2,S4′と比較する。ここで、取水ポンプ停止
検出手段21は取水ポンプ運転台数S1が設定値
S1′と等しくなければ浄水場の水処理流量に急
変が生じていると判断し異常信号を出力する。ま
た、着水流量異常検出手段22は着水流量S2ま
たは沈でん池総流入流量S3の変化が流量変化設
定値S2′以上のときに異常信号を出力する。水
位変化異常検出手段23は単位時間内の沈でん池
流出渠水位S4が設定値S4′以上のときに異常
信号を出力する。
As described above, in this apparatus, it is necessary to operate an appropriate number of filters 16 according to the water treatment flow rate of the water purification plant.Hereinafter, the operation of the apparatus of the present invention will be explained with reference to FIG. 3. When the device starts operating by turning on the power, as shown in step ST1, the water intake pump stop detection means 21, the water landing flow abnormality detection means 22, and the water level change abnormality detection means 2 are activated.
3 takes in the number of intake pumps in operation S1, the landing flow rate S2 (or the total inflow flow rate of the sedimentation basin S3), and the sedimentation basin outflow channel water level S4, and sets the respective set values S1' and S.
2, compare with S4'. Here, if the number S1 of water intake pumps in operation is not equal to the set value S1', the water intake pump stop detection means 21 determines that a sudden change has occurred in the water treatment flow rate at the water purification plant, and outputs an abnormal signal. Further, the landing flow rate abnormality detection means 22 outputs an abnormal signal when the change in the landing flow rate S2 or the total inflow flow rate S3 of the sedimentation basin is equal to or larger than the flow rate change set value S2'. The water level change abnormality detection means 23 outputs an abnormal signal when the sedimentation pond outflow channel water level S4 within a unit time is equal to or higher than a set value S4'.

以上のようにして各検出手段21〜23の何れ
か1つから異常信号が出力されると、制御タイミ
ング決定手段24はステツプST2〜ST4の処理を
行つてろ過池16の起動または停止のタイミング
を決定する。すなわち、制御タイミング決定手段
24は、水位計32からの時間tにおける沈でん
池流出渠水位をh(t)、制御水位上限設定値
HL、制御水位下限設定値LLとすると、ステツプ
ST2において、 h<LLまたはHL<h ……(2) の関係にあるか否かを判断し、上記関係にあれば
ステツプST3に移行し観測時間DT内での沈でん
池流出渠水位の変化量DHを演算する。
When an abnormal signal is output from any one of the detection means 21 to 23 as described above, the control timing determination means 24 performs steps ST2 to ST4 to determine the timing for starting or stopping the filter 16. decide. In other words, the control timing determining means 24 sets the water level of the sedimentation basin outflow channel at time t from the water level meter 32 to h(t) and the control water level upper limit set value.
If HL and control water level lower limit set value LL, then step
In ST2, it is determined whether the relationship h<LL or HL<h...(2) exists, and if the above relationship exists, the process moves to step ST3 and the amount of change in the water level of the sedimentation basin outflow channel within the observation time DT is determined. Calculate DH.

DH−h(t)−h(t−DT) ……(3) そして、沈でん池流出渠水位の変化量DHを求
めたならば、時間Tを求める。
DH-h(t)-h(t-DT)...(3) Then, once the amount of change DH in the water level of the sedimentation basin outflow channel is determined, the time T is determined.

T=|(DT/DH)|・α ……(4) 但し、αは制御パラメータ(定数)である。 T=|(DT/DH)|・α……(4) However, α is a control parameter (constant).

このステツプST3において時間Tを求めたなら
ば、ステツプST4に基づいて過去時間Tの間にろ
過池16の起動または停止を行つていなければ制
御タイミングであると決定し、制御タイミング信
号を出力する。過去時間T以内にろ過池16の起
動または停止を行つている場合には制御タイミン
グ信号を出力しない。
Once the time T has been determined in step ST3, if the filter 16 has not been started or stopped during the past time T based on step ST4, it is determined that it is the control timing, and a control timing signal is output. . If the filter 16 has been started or stopped within the past time T, no control timing signal is output.

ここで、起動・停止池数決定手段25は制御タ
イミング信号を受けると起動または停止するろ過
池数を決定する(ステツプST5)。この起動また
は停止池数△Nは、 (a) ろ過池起動時 △N=(DH・A)/(DT・Qs)・β ……(5) (b) ろ過池停止時 △N=(DH・A)/(DT・Qe)・β ……(6) で表わされる。上式においてAは沈でん池流出渠
面積、Qsはろ過池起動時のろ過流量平均値、Qe
はろ過池停止時のろ過流量平均値、βは制御パラ
メータである。
Here, the start/stop filter number determining means 25 determines the number of filter filters to be started or stopped upon receiving the control timing signal (step ST5). This number of starting or stopping ponds △N is: (a) When the filter starts △N = (DH・A)/(DT・Qs)・β ……(5) (b) When the filter stops △N=(DH・A)/(DT・Qe)・β ...(6) It is expressed as. In the above formula, A is the sedimentation basin outflow conduit area, Qs is the average filtration flow rate at the time of starting the filtration basin, and Qe
is the average value of the filtration flow rate when the filtration basin is stopped, and β is the control parameter.

以上のようにして起動・停止池数△Nが決定さ
れると、この決定池数△Nに基づいて起動・停止
池決定手段26はステツプST6〜ST8に基づいて
起動または停止するろ過池を決定する。このろ過
池の決定は各ろ過池16の弁開閉状態信号S1
1、ろ抗信号S12、ろ過流量S13および池決
定基準設定値S14等を取込み、これらの信号S
11〜S13から何れのろ過池16がどれ位の時
間の間停止または稼働あるいは疲労状態にあるか
を把握し、例えば停止時間が基準設定値S14を
越えている場合には最も停止時間の長いろ過池1
6から短いろ過池16へと順次△Nのろ過池を選
択し、これら△Nのろ過池16に対しろ過池起動
指令(△N>0の時)を操作端制御部30へ送出
する。
When the number of starting/stopping ponds ΔN is determined as described above, the starting/stopping pond determining means 26 determines the filtration pond to be started or stopped based on the determined number of ponds ΔN in steps ST6 to ST8. do. This determination of the filter is determined by the valve opening/closing status signal S1 of each filter 16.
1. Take in the filtration signal S12, filtration flow rate S13, pond determination standard set value S14, etc., and use these signals S
From 11 to S13, it is determined for how long which filter 16 has been stopped, in operation, or in a fatigued state, and for example, if the stoppage time exceeds the standard set value S14, the filter with the longest stoppage time is selected. Pond 1
6 to the short filters 16, and sends a filter activation command (when ΔN>0) to the operating end control unit 30 for these ΔN filters 16.

一方、停止池の決定は、最も稼働時間の長いろ
過池16から△N池数分だけ順次ろ過池16を選
択し、これら△Nのろ過池16に対してろ過池停
止指令(△<0の時)を操作端制御部30へ送出
する。ここで、操作端制御部30は決定したろ過
池16に対し過起動指令またはろ過池停止指令を
与えて当該ろ過池16を起動または停止し、常に
各ろ過池16のろ過流量を設定範囲内でろ過運転
する。
On the other hand, to determine the stop ponds, filters 16 are sequentially selected for the number of △N filters starting from the filter 16 with the longest operating time, and a filter stop command is issued to these △N filters 16 (for △<0). time) is sent to the operating end control section 30. Here, the operating end control unit 30 gives an overstart command or a filter stop command to the determined filter 16 to start or stop the filter 16, and always keeps the filtration flow rate of each filter 16 within the set range. Run filtration.

なお、具体例をもつて説明すると、例えば着水
流量の急激な減少により着水流量異常検出手段2
2から異常信号が出力されると、この異常信号を
受けて制御タイミング決定手段24は観測時間
DTの間に沈でん池渠水位がDH1だけ変化したと
すると、前記(4)式から時間T1は、 T1=(DT/DH1)・α ……(4)′ が得られる。この式から浄水場の水処理流量の変
化が大きい場合にはT1の値が小さくなり、逆に
浄水場の水処理流量の変化が小さい場合にはT1
の値が大きくなる。このことは、浄水場の水処理
流量の変化が大きい場合には短い周期でろ過池1
6の起動または停止が行われ、逆に浄水場の水処
理流量の変化が小さい場合には長い周期でろ過池
16の起動または停止が行われる。特に、浄水場
の水処理流量の変化が極めて大きい場合にはT1
の値はさらに小さくなつて制御周期以下になる。
この場合、停止するろ過池16の池数△N1は上
記(6)式から △N1=(DH1・A)/(DT・Qe)・β ……(6)′ となる。すなわち、浄水場の水処理流量の変化が
大きい場合には起動または停止するろ過池数△N
が増加し、ろ過流量が大幅に変化するように制御
する。
In addition, to explain with a specific example, for example, due to a sudden decrease in the landing flow rate, the landing flow abnormality detection means 2
When an abnormal signal is output from 2, the control timing determining means 24 receives this abnormal signal and determines the observation time.
Assuming that the sedimentation pond water level changes by DH1 during DT, the time T1 can be obtained from equation (4) as follows: T1=(DT/DH1)・α...(4)′. From this equation, if the change in the water treatment flow rate at the water treatment plant is large, the value of T1 will be small, and conversely, if the change in the water treatment flow rate at the water treatment plant is small, the value of T1 will be small.
The value of increases. This means that when there are large changes in the water treatment flow rate at a water treatment plant, the filtration
On the other hand, when the change in the water treatment flow rate at the water purification plant is small, the filtration basin 16 is started or stopped at long intervals. In particular, T1
The value of becomes even smaller and becomes less than the control period.
In this case, the number ΔN1 of the filters 16 to be stopped is calculated from the above equation (6) as follows: ΔN1=(DH1・A)/(DT・Qe)・β (6)′. In other words, if there is a large change in the water treatment flow rate at the water treatment plant, the number of filtration ponds to be started or stopped △N
is controlled so that the filtration flow rate increases and the filtration flow rate changes significantly.

従つて、以上のような実施例によれば、例えば
沈でん池流出渠水位等のプロセス状態信号から浄
水場の水処理流量に大きな変化が生じていること
を検出すると、例えば沈でん池流出渠水位等の要
素に基づいて自動的に起動または停止する池数を
決定し、各ろ過池16…の停止時間または稼働時
間の長さから前記池数に相当するろ過池16を選
択して起動または停止するようにしたので、浄水
場の水処理流量の大幅な変動に対して短周期でろ
過池16の起動または停止を行うことができ、し
かも常に水処理流量に見合つた稼働ろ過池数でろ
過洗浄することが可能となり、ろ過池16のろ床
16aが空気中に触れる心配がなくなり安定な運
転を確保できる。また、各ろ過池16の中から稼
働状態を考慮しつつ決定池数分だけ選択して起動
または停止制御するので、各ろ過池16の稼働時
間を平均化することができろ過能力等の点からも
望ましい。
Therefore, according to the embodiments described above, when it is detected that a large change has occurred in the water treatment flow rate of the water treatment plant from the process status signal such as the water level of the sedimentation pond outflow conduit, for example, the water level of the sedimentation pond outflow conduit, etc. The number of filters to be automatically started or stopped is determined based on the factors, and the filters 16 corresponding to the number of filters are selected and started or stopped based on the length of the stop time or operating time of each filter 16. As a result, the filter 16 can be started or stopped in a short period in response to large fluctuations in the water treatment flow rate at the water treatment plant, and the filter cleaning is always performed with the number of active filter basins commensurate with the water treatment flow rate. Therefore, there is no need to worry about the filter bed 16a of the filter basin 16 coming into contact with the air, and stable operation can be ensured. In addition, since only the determined number of filters are selected from among the filters 16 and controlled to start or stop, taking into account the operating state, the operating time of each filter 16 can be averaged, and from the point of view of filtration capacity, etc. is also desirable.

なお、本発明は上記実施例に限定されるもので
はない。例えば第4図に示すように各ろ過池1
6,…にろ過池流量調節弁41,…が設備されて
いる場合、各ろ過池16ごとにろ過流量制御装置
42,…を設け、ろ過流量S13およびろ過流量
目標値S41に基づいて例えばPID制御を行い、
得られた操作出力により前記ろ過流量調節弁41
の開度を調節し、各ろ過池16のろ過流量がろ過
流量目標値となるように制御してもよい。
Note that the present invention is not limited to the above embodiments. For example, as shown in Figure 4, each filtration basin 1
6,... are equipped with filtration flow rate control valves 41,..., each filter 16 is provided with a filtration flow rate control device 42,..., and performs, for example, PID control based on the filtration flow rate S13 and the filtration flow rate target value S41. and
The obtained operation output controls the filtration flow rate control valve 41.
You may control the filtration flow rate of each filtration basin 16 so that it becomes a filtration flow rate target value by adjusting the opening degree of the filtration basin 16 .

このような実施例の構成によれば、ろ過流量制
御装置42のPID演算制御により各ろ過池16の
ろ過流量qiがろ過流量目標値S41となるように
制御され、その結果、上記(1)式のΣqiの項は一定
値となり、かつ、前述したように浄水場の水処理
流量に応じて起動または停止すべき池数が決定さ
れ、この池数に基づいて各ろ過池16を適宜選択
して起動または停止制御を行うものである。
According to the configuration of such an embodiment, the filtration flow rate qi of each filter basin 16 is controlled to be the filtration flow rate target value S41 by the PID calculation control of the filtration flow rate control device 42, and as a result, the above equation (1) The term Σqi is a constant value, and as mentioned above, the number of ponds to be started or stopped is determined according to the water treatment flow rate of the water treatment plant, and each filter basin 16 is selected as appropriate based on this number of ponds. It performs start or stop control.

次に、第5図は同じく本発明装置の他の実施例
を説明する構成図である。すなわち、この実施例
は、ろ過池16にろ過流量調節弁41が設備され
ている場合、前記ろ過流量制御装置42のほかに
水位制御装置51を設け、この水位制御装置51
において沈でん池流出渠水位S4と沈でん池流出
渠水位目標値S51とに基づいて各ろ過池16,
…のろ過流量目標値S41を自動的に決定し前記
ろ過流量制御装置42へ供給する構成であつても
よい。つまり、水位制御装置51は沈でん池流出
渠の水位が上昇したときろ過流量目標値S41を
増加させ、逆に沈でん池流出渠の水位が下降した
ときろ過流量目標値S41を減少させるように作
用させながらろ過流量を制御する。
Next, FIG. 5 is a block diagram illustrating another embodiment of the apparatus of the present invention. That is, in this embodiment, when the filtration flow rate control valve 41 is installed in the filtration basin 16, a water level control device 51 is provided in addition to the filtration flow rate control device 42, and this water level control device 51
In each filter basin 16, based on the sedimentation pond outflow conduit water level S4 and the sedimentation basin outflow conduit water level target value S51
The filtration flow rate target value S41 may be automatically determined and supplied to the filtration flow rate control device 42. In other words, the water level control device 51 increases the filtration flow rate target value S41 when the water level of the sedimentation pond outflow drain rises, and conversely acts to decrease the filtration flow rate target value S41 when the water level of the sedimentation basin outflow drain decreases. while controlling the filtration flow rate.

今、i号ろ過池16iのろ過流量目標値を
Qref−iとする。このろ過池16iのろ過流量
には物理的に上下限があるので、ろ過流量目標値
Qref−iは次の式を満足させなければならない。
Now, the target value of filtration flow rate for No. I filtration basin 16i is
Let it be Qref-i. Since there are physically upper and lower limits to the filtration flow rate of this filtration basin 16i, the filtration flow rate target value
Qref-i must satisfy the following formula.

Qmin−i≦Qref−i≦Qmax−i ……(7) 但し、Qmin−iはi号ろ過池16iの最小ろ
過流量目標値、Qmax−iはi号ろ過池16iの
最大ろ過流量目標値である。従つて、水位制御装
置51では沈でん池流出渠の水位に基づいて算出
されたろ過流量目標値Qref−iが上限値Qmax−
iまたは下限値Qmin−iを越える場合、つまり
上記(7)式が満足されない場合にはQref−iが上
限値Qmax−iまたは下限値Qmin−iでリミツ
トする。この結果、(1)式のΣqiの項はΣQmax−
i(または下限値Qmin−i)以上または以下の
値にリセツトされ、これを越える水処理流量の変
化分で沈でん池流出渠の水位が変化し、浄水場の
水処理流量に応じて稼働ろ過池数が制御すること
ができる。
Qmin-i≦Qref-i≦Qmax-i ...(7) However, Qmin-i is the minimum filtration flow rate target value of No. I filter 16i, and Qmax-i is the maximum filtration flow rate target value of No. I filter 16i. be. Therefore, in the water level control device 51, the filtration flow rate target value Qref-i calculated based on the water level of the sedimentation basin outflow channel is set to the upper limit value Qmax-.
Qref-i is limited to the upper limit Qmax-i or the lower limit Qmin-i when it exceeds the upper limit Qmin-i or the lower limit Qmin-i, that is, when the above equation (7) is not satisfied. As a result, the term Σqi in equation (1) becomes ΣQmax−
i (or the lower limit value Qmin-i), the water level in the sedimentation basin outflow channel will change depending on the amount of change in the water treatment flow rate that exceeds this value, and the operating filtration pond will change depending on the water treatment flow rate at the water treatment plant. The number can be controlled.

その他、本発明はその要旨を逸脱しない範囲で
種々変形して実施できる。
In addition, the present invention can be implemented with various modifications without departing from the gist thereof.

[発明の効果] 以上詳記したように本発明によれば、浄水場の
種々のプロセス状態信号からプロセスの異常を検
出したとき、観測時間内での沈でん池流出渠水位
の変化量に応じて制御タイミング時間を可変しな
がら起動または停止するろ過池数を決定するの
で、浄水場の水処理流量が大幅に変動したときで
も安定、かつ、安全運転を考慮しながら適正なろ
過池数を決定でき、よつて、人手による介入なし
で各ろ過池を適正な状態で継続運転でき、ろ過池
の水位の低下を未然に回避してろ過池のろ床の露
出を防ぎ、かつ、沈でん池流出渠の水位異常高に
よるオーバーフローを防止し、浄水場の安定な運
転を確保できる浄水場のろ過池数制御装置を提供
できる。
[Effects of the Invention] As described in detail above, according to the present invention, when a process abnormality is detected from various process status signals of a water treatment plant, it is possible to detect a The number of filters to start or stop is determined while varying the control timing time, so even when the water treatment flow rate at the water treatment plant fluctuates significantly, the appropriate number of filters can be determined while considering stable and safe operation. Therefore, each filtration basin can be continuously operated in an appropriate state without manual intervention, and a drop in the water level of the filtration basin can be avoided and the exposure of the filter bed of the filtration basin can be prevented. It is possible to provide a filter number control device for a water purification plant that can prevent overflow due to abnormally high water levels and ensure stable operation of the water purification plant.

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

第1図ないし第3図は本発明装置の一実施例を
説明するために示したもので、第1図は装置全体
の構成図、第2図は浄水場の水位高低関係を説明
する模式図、第3図は本発明装置の動作を説明す
る処理手順図、第4図および第5図はそれぞれろ
過流量調節弁を設けた場合の他の実施例を示す構
成図である。 10……浄水場、12……取水ポンプ、13…
…着水井、14……沈でん池、15……沈でん池
流出渠、16……ろ過池、20……ろ過池数制御
装置、21……取水ポンプ停止検出手段、22…
…着水流量異常検出手段、23……水位変化異常
検出手段、24……制御タイミング決定手段、2
5……起動・停止池数決定手段、26……起動・
停止池決定手段、30……操作端制御部、41…
…ろ過流量調節弁、42……ろ過流量制御装置、
51……水位制御装置。
Figures 1 to 3 are shown to explain one embodiment of the device of the present invention. Figure 1 is a configuration diagram of the entire device, and Figure 2 is a schematic diagram explaining the relationship between water levels in a water purification plant. , FIG. 3 is a processing procedure diagram explaining the operation of the apparatus of the present invention, and FIGS. 4 and 5 are configuration diagrams showing other embodiments in which a filtration flow rate regulating valve is provided, respectively. 10...Water treatment plant, 12...Water intake pump, 13...
... Water landing well, 14 ... Sedimentation pond, 15 ... Sedimentation pond outflow channel, 16 ... Filtration pond, 20 ... Filter number control device, 21 ... Water intake pump stop detection means, 22 ...
... Water landing flow rate abnormality detection means, 23 ... Water level change abnormality detection means, 24 ... Control timing determination means, 2
5... Means for determining the number of starting/stopping ponds, 26... Starting/stopping
Stop pool determining means, 30... operating end control unit, 41...
...filtration flow rate control valve, 42...filtration flow rate control device,
51...Water level control device.

Claims (1)

【特許請求の範囲】 1 取水ポンプで取り込んだ原水に含まれる混濁
物質、浮遊物等を、着水井、沈でん池、沈でん池
流出渠および複数のろ過池を通して沈でん、ろ過
等による水処理を行い、その水処理流量に応じて
稼働するろ過池の池数を増減制御する浄水場のろ
過池数制御装置において、 前記沈でん池流出渠を含む前処理段階のプロセ
ス状態信号を取得するプロセス状態信号取得手段
と、このプロセス状態信号取得手段で取得された
プロセス状態信号を用いて浄水場プロセスの異常
状態を検出する異常検出手段と、この異常検出手
段から異常検出信号を受けたとき、観測時間内で
の前記沈殿でん池流出渠の水位変化量から制御タ
イミング時間を決定し、この制御タイミング時間
に基づいて起動または停止するろ過池の池数を決
定し、この池数に基づいて起動または停止するろ
過池を決定するろ過池数決定手段とを備えたこと
を特徴とする浄水場のろ過池数制御装置。 2 プロセス状態信号取得手段は、前記取水ポン
プの運転台数、前記着水井の着水流量、沈でん池
への沈でん池総流入流量および前記沈でん池流出
渠の水位変化のうち少なくとも沈でん池流出渠の
水位変化を取得するものである特許請求の範囲第
1項記載の浄水場のろ過池数制御装置。 3 ろ過池数決定手段は、ある観測時間内での沈
でん池流出渠水位の変化量、沈でん池流出渠面積
等のデータを用いて池数を決定するものである特
許請求の範囲第1項記載の浄水場のろ過池数制御
装置。 4 ろ過池数決定手段は、前記池数に基づいて各
ろ過池の弁開閉状態信号、ろ抗信号、ろ過流量お
よび池決定基準設定値等を用いてろ過池の停止ま
たは稼働状態を把握し、その停止時間および稼働
時間から起動または停止するろ過池を順次決定し
ていくものである特許請求の範囲第1項記載の浄
水場のろ過池数制御装置。
[Scope of Claims] 1. Processing water such as turbid substances, suspended matter, etc. contained in raw water taken in by a water intake pump through sedimentation, filtration, etc. through a landing well, a sedimentation pond, a sedimentation pond outflow drain, and a plurality of filtration ponds, In a filter number control device for a water purification plant that increases or decreases the number of filters operated according to the water treatment flow rate, a process status signal acquisition means for acquiring a process status signal of a pretreatment stage including the sedimentation basin outflow conduit. and an abnormality detection means for detecting an abnormal state of the water purification plant process using the process state signal acquired by the process state signal acquisition means; A control timing time is determined from the amount of water level change in the sedimentation basin outflow conduit, the number of filtration ponds to be started or stopped is determined based on this control timing time, and filtration to be started or stopped based on this number of ponds. A device for controlling the number of filtration ponds in a water purification plant, comprising: means for determining the number of filtration ponds for determining the number of filtration ponds. 2. The process status signal acquisition means is configured to detect at least the water level of the settling basin outflow drain among the number of operating water intake pumps, the landing flow rate of the landing well, the total flow rate of the settling basin into the settling basin, and the water level change of the settling basin outflow drain. A filter number control device for a water purification plant according to claim 1, which obtains changes. 3. The means for determining the number of filtration ponds determines the number of ponds using data such as the amount of change in the water level of the sedimentation basin outflow channel and the area of the sedimentation basin outflow conduit within a certain observation time. A device to control the number of filtration ponds at a water treatment plant. 4. The filtration basin number determination means grasps the stoppage or operating status of the filtration basins based on the number of basins, using the valve opening/closing state signal, filtration signal, filtration flow rate, basin determination standard set value, etc. of each filtration basin, The device for controlling the number of filters in a water purification plant according to claim 1, which sequentially determines which filters to start or stop based on the stop time and operation time.
JP62300408A 1987-11-28 1987-11-28 Apparatus for controlling number of filter basin in purification plant Granted JPH01143678A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62300408A JPH01143678A (en) 1987-11-28 1987-11-28 Apparatus for controlling number of filter basin in purification plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62300408A JPH01143678A (en) 1987-11-28 1987-11-28 Apparatus for controlling number of filter basin in purification plant

Publications (2)

Publication Number Publication Date
JPH01143678A JPH01143678A (en) 1989-06-06
JPH0471596B2 true JPH0471596B2 (en) 1992-11-16

Family

ID=17884436

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62300408A Granted JPH01143678A (en) 1987-11-28 1987-11-28 Apparatus for controlling number of filter basin in purification plant

Country Status (1)

Country Link
JP (1) JPH01143678A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0093152B1 (en) * 1981-11-10 1986-03-26 Ncr Corporation Sheet handling apparatus

Also Published As

Publication number Publication date
JPH01143678A (en) 1989-06-06

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