JPH0333395B2 - - Google Patents
Info
- Publication number
- JPH0333395B2 JPH0333395B2 JP61033593A JP3359386A JPH0333395B2 JP H0333395 B2 JPH0333395 B2 JP H0333395B2 JP 61033593 A JP61033593 A JP 61033593A JP 3359386 A JP3359386 A JP 3359386A JP H0333395 B2 JPH0333395 B2 JP H0333395B2
- Authority
- JP
- Japan
- Prior art keywords
- flow rate
- water level
- wastewater
- return flow
- wastewater return
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 85
- 239000002351 wastewater Substances 0.000 claims description 51
- 238000004140 cleaning Methods 0.000 claims description 39
- 238000001914 filtration Methods 0.000 claims description 14
- 238000000746 purification Methods 0.000 claims description 13
- 238000001514 detection method Methods 0.000 claims description 9
- 230000002123 temporal effect Effects 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- 238000000034 method Methods 0.000 description 6
- 230000008569 process Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 239000008213 purified water Substances 0.000 description 4
- 239000003657 drainage water Substances 0.000 description 2
- 230000008570 general process Effects 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Description
【発明の詳細な説明】
〔発明の目的〕
(産業上の利用分野)
本発明はろ過池洗浄時の着水井への排水返送流
量の変動を抑えて浄水水質を向上させる浄水場の
排水返送流量制御装置に関するものである。[Detailed Description of the Invention] [Object of the Invention] (Industrial Field of Application) The present invention is directed to improving the quality of purified water by suppressing fluctuations in the flow rate of wastewater returned to the receiving well during filter cleaning. This relates to a control device.
(従来の技術)
浄水場の一般的なプロセス構成を第5図に示
す。同図において、原水1は着水井2に到着し、
常時は沈殿池3、ろ過池4および浄水池5を経て
需要先6に供給される。(Prior Art) Figure 5 shows a general process configuration of a water purification plant. In the same figure, raw water 1 arrives at landing well 2,
Water is normally supplied to a consumer 6 via a settling tank 3, a filtration tank 4, and a water purification tank 5.
ろ過池4の洗浄時には、洗浄のための水が浄水
池5からろ過池4に供給され、洗浄排水は排水池
8に流入し、返送ポンプ9によつて着水井2に返
送されて再利用される。 When cleaning the filtration basin 4, water for cleaning is supplied from the water purification basin 5 to the filtration basin 4, and the cleaning wastewater flows into the drainage basin 8, and is returned to the receiving well 2 by the return pump 9 to be reused. Ru.
(発明が解決しようとする問題点)
従来は排水池8の水位hを水井計12によつて
検出し、水位hが一定となる排水返送流量目標値
Qrをあたえ、流量計11で検出した排水返送量
Qbをフイードバツクして流量制御装置7を介し
て流量調整弁10を制御しているが、ろ過池の洗
浄時は排水返送量Qbが増大し、結果として着水
井2に過大な排水が返送されて浄水の水質を低下
させるという問題がある。(Problems to be Solved by the Invention) Conventionally, the water level h of the drainage pond 8 is detected by the water well gauge 12, and a target value of the wastewater return flow rate at which the water level h becomes constant is determined.
Amount of wastewater returned by applying Q r and detected by flow meter 11
The flow rate adjustment valve 10 is controlled via the flow rate control device 7 by feeding back Q b , but when cleaning the filtration basin, the amount of wastewater returned Q b increases, and as a result, an excessive amount of wastewater is returned to the landing well 2. There is a problem that the quality of purified water deteriorates.
本発明は上記の問題点を解決するためになされ
たもので、排水池の水位を許容範囲に制限しなが
ら適正な水質を得ることのできる浄水場の排水返
送流量制御装置の提供を目的とする。 The present invention has been made to solve the above problems, and aims to provide a wastewater return flow rate control device for a water purification plant that can obtain appropriate water quality while limiting the water level in a drainage pond to an allowable range. .
(問題点を解決するための手段)
本発明は、排水池の水位を時間に対応して記憶
させる水位追跡手段と、その記憶値に基いて排水
池水位の極値を検出する極値検出手段と、ろ過池
の洗浄周期、排水池水位の許容限度を設定する条
件設定手段と、排水返送流量の変動範囲に応じて
設けられる制御パラメータ演算手段と、上記極値
検出手段および条件設定手段の出力、または、こ
れに制御パラメータ演算手段を加えた各出力に基
いて排水返送流量目標値を演算する流量目標値演
算手段とを備えたものである。
(Means for Solving the Problems) The present invention provides a water level tracking means for storing the water level of a drainage pond in correspondence with time, and an extreme value detection means for detecting the extreme value of the water level of the drainage pond based on the stored value. , a condition setting means for setting the cleaning cycle of the filtration basin and the permissible limit of the water level of the drainage basin, a control parameter calculation means provided according to the fluctuation range of the wastewater return flow rate, and the outputs of the extreme value detection means and the condition setting means. , or a flow rate target value calculation means for calculating a wastewater return flow rate target value based on each output obtained by adding a control parameter calculation means to the control parameter calculation means.
(作用)
この発明においては、水位追跡手段に記憶され
た排水池の水位データに基いて極値検出手段が排
水池水位の極値を検出し、さらに、その検出極値
に基いて制御パラメータ演算手段が制御パラメー
タを演算する一方、条件設定手段によつてろ過池
の洗浄周期、排水池水位の許容限度を設定し、流
量目標値演算手段が上記検出極値および設定値に
基いて排水返送流量目標を演算するか、あるい
は、検出極値、設定値および制御パラメータに基
いて排水返送流量目標値を演算し、この排水返送
流量目標値に従つて排水返送流量を制御する。(Operation) In this invention, the extreme value detection means detects the extreme value of the drainage pond water level based on the water level data of the drainage pond stored in the water level tracking means, and further calculates the control parameters based on the detected extreme value. While the means calculates the control parameters, the condition setting means sets the cleaning cycle of the filtration basin and the permissible limit of the water level of the drainage basin, and the flow rate target value calculating means calculates the wastewater return flow rate based on the detected extreme value and set value. Either a target is calculated, or a wastewater return flow rate target value is calculated based on the detected extreme value, set value, and control parameters, and the wastewater return flow rate is controlled in accordance with this wastewater return flow rate target value.
(実施例)
第1図は本発明の一実施例の構成を、一般的な
浄水場のプロセスと併せて示したブロツク図であ
り、図中第5図と同一の符号を付したものはそれ
ぞれ同一の要素を示している。(Embodiment) Fig. 1 is a block diagram showing the configuration of an embodiment of the present invention together with the process of a general water purification plant. Showing the same element.
ここで、原水1は着水井2に到着し、常時は沈
殿池3、ろ過池4および浄水池5を経て需要先6
に供給される。また、ろ過池4の洗浄時には、浄
水池5の水をろ過池4に返送し、洗浄に供された
洗浄排水は排水池8に流入し、さらに、着水井2
に戻されて再利用される。 Here, raw water 1 arrives at a receiving well 2, and normally passes through a settling tank 3, a filtration tank 4, and a water purification tank 5 before reaching a demand destination 6.
is supplied to Furthermore, when cleaning the filtration basin 4, the water in the water purification basin 5 is returned to the filtration basin 4, and the washed wastewater used for cleaning flows into the drainage basin 8, and further, the water from the water receiving well 2
returned to and reused.
ところで、この洗浄過程で着水井2に戻す排水
返送流量の変化を小さく抑えるために流量制御装
置7と洗浄制御装置13とが設けられている。 Incidentally, a flow rate control device 7 and a cleaning control device 13 are provided to suppress changes in the flow rate of waste water returned to the landing well 2 during this cleaning process.
このうち、流量制御装置7は、排水池8の水位
hを検出する水位計12、排水返送流量を検出す
る流量計11、および後述する流量目標値演算手
段24の各出力に基いて返送ポンプ9と流量調整
弁10を制御している。 Of these, the flow rate control device 7 controls the return pump 9 based on the respective outputs of a water level meter 12 that detects the water level h of the drainage pond 8, a flow meter 11 that detects the wastewater return flow rate, and a flow rate target value calculation means 24, which will be described later. and controls the flow rate adjustment valve 10.
また、洗浄制御装置13は、水位計12、条件
設定手段25の各出力に基づき、洗浄に必要な水
をろ過池4に供給するべく流量調整弁やポンプを
制御するが、その詳しい制御内容は本発明に直接
関係しないので説明を省略する。 Further, the cleaning control device 13 controls the flow rate adjustment valve and pump to supply the water necessary for cleaning to the filter basin 4 based on the outputs of the water level gauge 12 and the condition setting means 25, but the detailed control contents are as follows. Since it is not directly related to the present invention, the explanation will be omitted.
一方、上述した排水返送流量目標値Qrを演算
するために、電子計算機を用いた制御装置20a
が用いられる。この制御装置20aは、水位計1
2によつて検出される排水池8の水位を、例え
ば、洗浄周期の1.5倍程度の期間に亘つて記憶さ
せる水位追跡手段21と、この水位追跡手段21
の記憶値から排水値水位極大値Hnaxを求める極
値検出手段22と、この極値検出手段22の検出
極値および条件設定手段25の洗浄周期、排水池
水位を所定の算式に代入して返送流量目標値Qr
を演算する流量目標値演算手段24とで構成され
ている。 On the other hand, in order to calculate the above-mentioned wastewater return flow rate target value Q r , a control device 20a using an electronic computer
is used. This control device 20a includes a water level gauge 1
a water level tracking means 21 for storing the water level of the drainage pond 8 detected by the drain pond 8 for a period of, for example, about 1.5 times the cleaning cycle;
The extreme value detecting means 22 calculates the maximum value H nax of the drainage water level from the stored value, and the extreme value detected by the extreme value detecting means 22, the cleaning cycle of the condition setting means 25, and the water level of the drainage pond are substituted into a predetermined formula. Return flow rate target value Q r
The target flow rate calculation means 24 calculates the flow rate target value.
以下、この実施例の概略動作を第2図のフロー
チヤートをも参照して説明する。 The general operation of this embodiment will be explained below with reference to the flowchart of FIG.
先ず、ステツプ100で水位追跡手段21を構成
するメモリの初期化、および、諸設定値の初期化
を行なう。続いて、実際の制御プログラムに移
り、ステツプ101では、洗浄周期設定値ΔT、排
水池水位の上限設定値Hhigh、下限設定値Hlpw、
および、排水池水位hを読込む。ステツプ102で
は、排水池水位の変化傾向を得るために排水池水
位hを水位追跡手段21に記憶させる。この水位
追跡手段21は下記の手順によつて順次データを
シフトさせ得るシフトレジスタによつて構成され
ており、洗浄周期の1.5倍程度に亘つて排水池水
位を記憶している。 First, in step 100, the memory constituting the water level tracking means 21 and various setting values are initialized. Next, the program moves to the actual control program, and in step 101, the cleaning cycle set value ΔT, the upper limit set value H high of the drainage pond water level, the lower limit set value H lpw ,
And read the drainage pond water level h. In step 102, the water level h of the drainage pond is stored in the water level tracking means 21 in order to obtain the change trend of the water level of the drainage pond. The water level tracking means 21 is composed of a shift register that can sequentially shift data according to the following procedure, and stores the water level of the drainage pond for about 1.5 times the cleaning cycle.
for n=1 to N−1 do H(n+1)←H(n); H(1)←h; ただし H(i):シフトレジスタを構成する配列 N:配列H(i)の大きさ である。for n=1 to N−1 do H(n+1)←H(n); H(1)←h; however H(i): Array configuring shift register N: Size of array H(i) It is.
次に、ステツプ103では、極値検出手段22に
よつて、排水池水位の極大値を求めるが、この場
合、次式を満足する水位を排水池水位の極大値
Hnaxとする。 Next, in step 103, the maximum value of the water level of the drainage pond is determined by the extreme value detection means 22. In this case, the maximum value of the water level of the drainage pond is determined as
H nax .
H(1)≦H(2)かつH(3)<H(2) …(1)
Hnax←H(2)
続いて、ステツプ104では、ステツプ103で求め
た排水池水位の極大値Hnaxに基づき、次式を用
いて排水返送流量目標値Qrを演算する。H(1)≦H(2) and H(3)<H(2) …(1) H nax ←H(2) Next, in step 104, the maximum value H nax of the drainage pond water level obtained in step 103 is determined. Based on this, calculate the wastewater return flow rate target value Q r using the following formula.
Qr=(Hnax−Hlpw)・A/ΔT・α …(2) ただし A:排水池断面積〔m2〕 Hnax:排水池水位極大値〔m〕 Hlpw:排水池水位下限設定値〔m〕 ΔT:ろ過池洗浄周期〔h〕 α:制御パラメータ Qr:排水返送流量目標値〔m3/h〕 である。Q r = (H nax − H lpw )・A/ΔT・α …(2) where A: Drainage pond cross-sectional area [m 2 ] H nax : Maximum value of drainage pond water level [m] H lpw : Drainage pond water level lower limit setting Value [m] ΔT: Filter cleaning cycle [h] α: Control parameter Q r : Target value of wastewater return flow rate [m 3 /h].
次いで、ステツプ106では上記排水返送流量目
標値Qrを流量制御装置7へオンライン出力する。
ここで、流量制御装置7はこれに加えられた排水
返送流量目標値Qrと流量計11によつて検出さ
れた排水返送流量Qbとが等しくなるように返送
ポンプ9および流量調整弁10を制御する。ま
た、ステツプ106では、図示しないタイマに設定
された時間を経過するまで時間待ちを行なう。こ
の時間は洗浄周期ΔTに対して略ΔT/10に設定
される。 Next, in step 106, the wastewater return flow rate target value Q r is output to the flow rate control device 7 online.
Here, the flow rate control device 7 controls the return pump 9 and the flow rate adjustment valve 10 so that the target value Q r of the waste water return flow rate added thereto is equal to the waste water return flow rate Q b detected by the flow meter 11 . Control. Further, in step 106, a time wait is performed until the time set in a timer (not shown) has elapsed. This time is set to approximately ΔT/10 with respect to the cleaning cycle ΔT.
第3図はこの流量制御における洗浄排水流量、
排水返送流量および排水池水位の時間的関係を示
したもので、複数のろ過池を周期ΔTで順次洗浄
する場合、洗浄排水流量が、同図aに示すよう
に、ΔQだけ変化したとする。この流量差ΔQに
応じて排水池の水位の極大値も変化するが、その
偏差分は1洗浄周期ΔTで吸収され、これによつ
て排水返送流量Qbは同図bに示すように一定に
保たれる。このとき、排水池8の水位hは同図c
に示すようにΔT時間に下限設定値Hlpwに向かう
ように変化する。 Figure 3 shows the cleaning drainage flow rate in this flow rate control.
This figure shows the temporal relationship between the wastewater return flow rate and the water level of the drainage basin. When multiple filter basins are sequentially washed at a period of ΔT, it is assumed that the washing wastewater flow rate changes by ΔQ, as shown in figure a. The maximum value of the water level in the drainage basin also changes according to this flow rate difference ΔQ, but this deviation is absorbed in one cleaning cycle ΔT, and as a result, the wastewater return flow rate Q b remains constant as shown in Figure b. It is maintained. At this time, the water level h of the drainage pond 8 is c
As shown in , it changes toward the lower limit set value H lpw during the ΔT time.
かくして、この実施例によれば、ろ過池毎に洗
浄排水流量に多少のばらつきがあつても、(2)式に
従つて排水返送流量目標値が決定されることか
ら、これらのばらつきは洗浄周期ΔTで吸収され
るため、排水返送流量Qbの変動を著しく低く抑
さえ得、これによつて浄水の水質低下を防ぎ得
る。 Thus, according to this embodiment, even if there is some variation in the flow rate of cleaning wastewater from filter to filter, the target value of the wastewater return flow rate is determined according to equation (2), so these variations can be eliminated by changing the cleaning cycle. Since it is absorbed at ΔT, fluctuations in the wastewater return flow rate Q b can be suppressed to a significantly low level, thereby preventing deterioration in the quality of purified water.
ところで、第3図cに示したように排水池水位
が時刻t1における極大値Hnax(1)と、時刻t2におけ
る極大値Hnax(0)との間にHnax(1)>Hnax(0)の関係
があつた場合、その変化傾向をも考慮して排水返
送流量目標値を決定すれば排水返送流量Qbの変
動分をさらに小さく抑えることができる。 By the way, as shown in Figure 3c, the water level of the drainage pond is H nax (1)>H between the maximum value H nax (1) at time t 1 and the maximum value H nax (0) at time t 2 . When there is a relationship of nax(0) , if the target value of the wastewater return flow rate is determined by taking into account its change tendency, the variation in the wastewater return flow rate Q b can be further suppressed.
第4図はかかる制御を行なうもう一つの実施例
であり、図中、第1図と同一の符号を付したもの
はそれぞれ同一の要素を示す。そして、制御装置
20bがパラメータ演算手段23を含む点が第1
図と異つている。 FIG. 4 shows another embodiment in which such control is carried out, and in the figure, the same reference numerals as in FIG. 1 indicate the same elements. The first point is that the control device 20b includes the parameter calculation means 23.
It is different from the illustration.
ここで、パラメータ演算手段23は(2)式に示す
制御パラメータαを決定するもので、次のように
して算出することができる。 Here, the parameter calculation means 23 determines the control parameter α shown in equation (2), and can be calculated as follows.
上記(2)式を汎化し、n回前の極大値までの影響
を考慮した返送流量目標値Qr(n)は、
Qr(n)=(Hnax(0)−Hlpw)・A/ΔT・α0
+(Hnax(1)−Hlpw)・A/ΔT・α1
+……………………
+(Hnax(o)−Hlpw)・A/ΔT・αo …(3)
と表わされる。 Generalizing the above formula (2), the return flow rate target value Q r (n) considering the influence up to the maximum value n times before is calculated as Q r (n) = (H nax(0) −H lpw )・A /ΔT・α 0 + (H nax(1) −H lpw )・A/ΔT・α 1 +…………………… +(H nax(o) −H lpw )・A/ΔT・α o ...(3) It is expressed as.
ただし、 Hnax(0):今回の極大値 Hnax(1):1回前の極大値 Hnax(o):n回前の極大値 α0、α1、……、αn:制御定数 である。 However, H nax(0) : Current maximum value H nax(1) : Previous maximum value H nax(o) : Local maximum value n times ago α 0 , α 1 , ..., αn : Control constant be.
ここで、一例としてn=1の場合の制御パラメ
ータαを求めるために、上記(2)式と(3)式とが等し
いとき次式が成立つ。 Here, as an example, in order to obtain the control parameter α in the case of n=1, when the above equations (2) and (3) are equal, the following equation holds true.
(Hnax(0)−Hlpw)・A/ΔT・α
=(Hnax(0)−Hlpw)・A/ΔT・α0
+(Hnax(1)−Hlpw)・A/ΔT・α1
=(Hnax(0)−Hlpw)・A/ΔT・(α0
+Hnax(1)−Hlpw/Hnax(0)−Hlpw・α1)…(4)
∴α=α0+Hnax(1)−Hlpw/Hnax(0)−Hlpw・α1 …(5)
この(5)式の右辺第1項は制御パラメータの定数
項、第2項は1回前の極大値に対する今回の極大
値の変化傾向を考慮した項である。(H nax(0) −H lpw )・A/ΔT・α = (H nax(0) −H lpw )・A/ΔT・α 0 + (H nax(1) −H lpw )・A/ΔT・α 1 = (H nax(0) −H lpw )・A/ΔT・(α 0 +H nax(1) −H lpw /H nax(0) −H lpw・α 1 )…(4) ∴α=α 0 +H nax(1) −H lpw /H nax(0) −H lpw・α 1 …(5) The first term on the right side of equation (5) is the constant term of the control parameter, and the second term is the previous term. This term takes into consideration the change tendency of the current maximum value with respect to the maximum value.
かくして、制御パラメータαは次式によつて与
えられる。 Thus, the control parameter α is given by the following equation.
α=f(α0、α1、…、αo、Hnax(0)、…、
Hnax(o)、Hlpw …(6)
以上のようにして制御パラメータが求められる
と、流量目標値演算手段24は、上記(2)式中の制
御パラメータαをも変数として排水返送流量目標
値Qrを演算する。α=f(α 0 , α 1 , ..., α o , H nax(0) , ..., H nax(o) , H lpw ...(6) When the control parameters are determined as above, the flow rate target value The calculating means 24 calculates the wastewater return flow rate target value Q r using the control parameter α in the above equation (2) as a variable as well.
かくして、第4図に示した実施例によれば、排
水池水位の変化傾向に応じて排水返送流量目標値
Qrを変えているので、第1図に示した実施例に
比較して排水返送流量Qbの変動分をさらに小さ
く抑えることができる。 Thus, according to the embodiment shown in FIG.
Since Q r is changed, the variation in the wastewater return flow rate Q b can be further suppressed compared to the embodiment shown in FIG.
ところで、浄水場の洗浄制御装置13(第1図
参照)では、排水池8のオーバーフローを防ぐこ
とを目的として、排水池水位hが上限設定値を超
えた場合には、洗浄を禁止するようにインタロツ
クされる。この洗浄制御装置13と、上記排水返
送流量制御装置を組合わせて上記(2)式の制御パラ
メータαを調整すると共に、ΔTを洗浄の基本周
期とすることにより、ろ過池洗浄排水流量のばら
つきを、洗浄周期の遅延によつて吸収すれば排水
返送流量の変動をさらに小さくすることができ
る。 By the way, in order to prevent the drainage pond 8 from overflowing, the cleaning control device 13 (see Fig. 1) of the water purification plant is designed to prohibit cleaning when the drainage pond water level h exceeds the upper limit setting value. Interlocked. This cleaning control device 13 is combined with the wastewater return flow rate control device to adjust the control parameter α in equation (2) above, and by setting ΔT as the basic cycle of cleaning, variations in the flow rate of filter cleaning drainage water can be reduced. If this is absorbed by delaying the cleaning cycle, the fluctuation in the waste water return flow rate can be further reduced.
すなわち、排水池水位上限設定値Hhighを適切
な値に設定することにより、洗浄禁止インタロツ
クが解除される時期よりも周期ΔTが短くなるよ
うにHhighおよびαを設定する。この結果、洗浄
制御装置13は、1回の洗浄終了からΔT時間後
には洗浄待ちとなり、排水池水位hがh=Hhigh
になると同時に洗浄を開始する。従つて、洗浄排
水流量が多い場合には、洗浄周期が長くなり、逆
に少ない場合には洗浄周期が短くなる。 That is, by setting the drainage pond water level upper limit set value H high to an appropriate value, H high and α are set so that the cycle ΔT is shorter than the time when the wash prohibition interlock is released. As a result, the cleaning control device 13 waits for cleaning after ΔT time from the end of one cleaning, and the water level h of the drainage pond becomes h=H high
Start cleaning at the same time. Therefore, when the flow rate of cleaning wastewater is large, the cleaning cycle becomes long, and conversely, when the flow rate is low, the cleaning cycle becomes short.
かくして、上記2つの実施例よりも、排水返送
流量の変動が小さくなる。 Thus, the fluctuation in the wastewater return flow rate is smaller than in the above two embodiments.
以上説明したように本発明によれば、ろ過池洗
浄水に対して、最も変動の小さい排水返送運用が
可能となつて水質処理プロセスに重大な影響をあ
たえる着水井への供給水の水量が安定し、これに
よつて浄水場の浄水水質を向上させることが可能
となる。
As explained above, according to the present invention, it is possible to operate the wastewater return operation with the least fluctuation in filter wash water, and the amount of water supplied to the receiving well, which has a significant impact on the water quality treatment process, is stabilized. This makes it possible to improve the quality of purified water at water treatment plants.
第1図は本発明の一実施例の構成を、浄水場の
プロセスと併せて示したブロツク図、第2図は同
実施例の作用を説明するためのフローチヤート、
第3図a,b,cは同じくその作用を説明するた
めのタイムチヤート、第4図は本発明の他の実施
例の構成を、浄水場のプロセスと併せて示したブ
ロツク図、第5図は浄水場の一般的なプロセスを
示した図である。
2……着水井、4……ろ過池、7……流量制御
装置、8……排水池、20a,20b……制御装
置、21……水位追跡手段、22……極値検出手
段、23……パラメータ演算手段、24……流量
目標値演算手段、25……条件設定手段。
Fig. 1 is a block diagram showing the configuration of an embodiment of the present invention together with the process of a water purification plant, and Fig. 2 is a flowchart for explaining the operation of the embodiment.
Figures 3a, b, and c are time charts for explaining the operation, Figure 4 is a block diagram showing the configuration of another embodiment of the present invention together with the water treatment plant process, and Figure 5. is a diagram showing the general process of a water treatment plant. 2...Water landing well, 4...Filtration basin, 7...Flow rate control device, 8...Drainage pond, 20a, 20b...Control device, 21...Water level tracking means, 22...Extreme value detection means, 23... . . . parameter calculation means, 24 . . . flow rate target value calculation means, 25 . . . condition setting means.
Claims (1)
井に返送する排水返送流量を制御する浄水場の排
水返送流量制御装置において、前記排水池の検出
水位を時間に対応して記憶させる水位追跡手段
と、この水位追跡手段の水位データに基いて排水
池水位の極値を検出する極値検出手段と、前記ろ
過池の洗浄周期と前記排水池水位の許容限度とを
設定する条件設定手段と、この条件設定手段の設
定値および前記極値検出手段の検出極値に基いて
排水返送流量目標値を演算する流量目標値演算手
段とを具備し、演算された前記排水返送目標値に
従つて排水返送流量を制御することを特徴とする
浄水場の排水返送流量制御装置。 2 ろ過池の洗浄排水を、排水池を経由して着水
井に返送する排水返送流量を制御する浄水場の排
水返送流量制御装置において、前記排水池の検出
水位を時間に対応して記憶させる水位追跡手段
と、この水位追跡手段の水位データに基いて排水
池水位の極値を検出する極値検出手段と、この極
値検出手段の検出極値の時間的変化率に基いて制
御パラメータを演算するパラメータ演算手段と、
前記ろ過池の洗浄周期と前記排水池水位の許容限
度とを設定する条件設定手段と、この条件設定手
段の設定値、前記極値検出手段の検出極値および
前記パラメータ演算手段の制御パラメータに基い
て排水返送流量目標値を演算する流量目標値演算
手段とを具備し、演算された前記排水返送流量目
標値に従つて排水返送流量を制御することを特徴
とする浄水場の排水返送流量制御装置。[Scope of Claims] 1. In a wastewater return flow rate control device for a water purification plant that controls the flow rate of washing wastewater from a filtration basin and returned to a receiving well via a drainage basin, the detected water level of the drainage basin is measured in time. water level tracking means to be stored in correspondence; extreme value detection means for detecting an extreme value of the water level of the drainage basin based on the water level data of the water level tracking means; and a cleaning cycle of the filtration basin and an allowable limit of the water level of the drainage basin. and a flow rate target value calculating means for calculating a wastewater return flow rate target value based on the set value of the condition setting means and the extreme value detected by the extreme value detecting means, A wastewater return flow rate control device for a water purification plant, characterized in that the wastewater return flow rate is controlled in accordance with a wastewater return target value. 2. A water level at which the detected water level of the drainage pond is stored in correspondence with time in a wastewater return flow rate control device of a water purification plant that controls the flow rate of wastewater return for returning cleaning wastewater from a filtration basin to a receiving well via a drainage basin. A tracking means, an extreme value detection means for detecting an extreme value of the drainage pond water level based on the water level data of the water level tracking means, and a control parameter is calculated based on a temporal change rate of the extreme value detected by the extreme value detection means. parameter calculation means for
a condition setting means for setting the cleaning cycle of the filtration basin and an allowable limit of the water level of the drainage basin; and a condition setting means based on the set value of the condition setting means, the detected extreme value of the extreme value detection means, and the control parameter of the parameter calculation means. A wastewater return flow rate control device for a water purification plant, comprising a flow rate target value calculating means for calculating a wastewater return flow rate target value based on the calculated wastewater return flow rate target value, and controlling the wastewater return flow rate in accordance with the calculated wastewater return flow rate target value. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61033593A JPS62191091A (en) | 1986-02-18 | 1986-02-18 | Waste water returning flow control system for water purification plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61033593A JPS62191091A (en) | 1986-02-18 | 1986-02-18 | Waste water returning flow control system for water purification plant |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62191091A JPS62191091A (en) | 1987-08-21 |
| JPH0333395B2 true JPH0333395B2 (en) | 1991-05-16 |
Family
ID=12390796
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61033593A Granted JPS62191091A (en) | 1986-02-18 | 1986-02-18 | Waste water returning flow control system for water purification plant |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62191091A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01292113A (en) * | 1988-05-13 | 1989-11-24 | Kuraray Co Ltd | Specific drawn yarn and production thereof |
| JP4829045B2 (en) * | 2006-08-29 | 2011-11-30 | 株式会社東芝 | Operation support system for water treatment plant |
-
1986
- 1986-02-18 JP JP61033593A patent/JPS62191091A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62191091A (en) | 1987-08-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5746233A (en) | Washing apparatus and method therefor | |
| JPH0333395B2 (en) | ||
| JPH0333396B2 (en) | ||
| JPH06230831A (en) | Water level control device | |
| JP2885449B2 (en) | Pump control device | |
| JPS6488722A (en) | Water level controller | |
| JPS60216145A (en) | Controlling device of electric water heater | |
| JPH024351B2 (en) | ||
| RU2090506C1 (en) | Method of controlling process of washing belite sludge with hot water | |
| JPH03237717A (en) | Washer for semiconductor substrate | |
| JPH04361821A (en) | Replenishing water controller for circulating water system | |
| JP2001017825A (en) | Flue gas desulfurization method and apparatus | |
| JPH04305206A (en) | Flocculating and filtration tank for water treatment | |
| SU1377835A1 (en) | Method of automatic control of cyclic reactor | |
| JPS5651217A (en) | Control of cleaning of filtration basin | |
| SU1563986A1 (en) | Apparatus for controlling heat-moisture treatment of ferroconcrete articles | |
| JPS61111186A (en) | Device for controlling flow rate of return waste water in water purifying plant | |
| JPS62216010A (en) | Controller for operation of water purification plant | |
| JP3665668B2 (en) | Operation method of batch activated sludge process | |
| JPS63100901A (en) | Liquid level correcting device | |
| JPH0779720B2 (en) | Sugar liquid flow rate setting method | |
| JP3196992B2 (en) | Chemical injection rate automatic control device | |
| SU1289522A1 (en) | Method of automatic regulation of evaporating apparatus | |
| JPS58196816A (en) | Control of filter basin group | |
| JPS5814837B2 (en) | Predictive control method for mixed liquid suspended solids concentration in activated sludge method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |