JPH025152B2 - - Google Patents
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- Publication number
- JPH025152B2 JPH025152B2 JP23244884A JP23244884A JPH025152B2 JP H025152 B2 JPH025152 B2 JP H025152B2 JP 23244884 A JP23244884 A JP 23244884A JP 23244884 A JP23244884 A JP 23244884A JP H025152 B2 JPH025152 B2 JP H025152B2
- Authority
- JP
- Japan
- Prior art keywords
- flow rate
- wastewater
- drainage
- return flow
- basin
- 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
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Description
【発明の詳細な説明】
〔発明の技術分野〕
本発明は、ろ過池を洗浄したり沈殿池から排泥
する時の排水流量の変動にかかわらず着水井への
返送流量の変動を最小にす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] [Technical Field of the Invention] The present invention minimizes fluctuations in the flow rate returned to the receiving well regardless of fluctuations in the flow rate of wastewater when cleaning a filter or draining a sedimentation basin. This invention relates to a wastewater return flow rate control device for a water treatment plant.
浄水場の一般的なプロセス構成を第2図に示
す。
Figure 2 shows the general process configuration of a water treatment plant.
第2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へ供給される。すなわち水の流れは矢印
15で示される。なお7はろ過池のろ床である。 In Figure 2, raw water 1 arrives at landing well 2,
Water is normally supplied to a consumer 6 via a sedimentation tank 3, a filtration tank 4, and a water purification tank 5. That is, the flow of water is indicated by arrows 15. Note that 7 is the filter bed of the filtration pond.
沈殿池3の排泥時は、排泥を含む水が沈殿池3
から引抜かれ、排水池8へ流入する。このときの
水の流れは矢印17で示される。 When the sedimentation tank 3 is drained, the water containing the drained sludge flows into the sedimentation tank 3.
It is pulled out from the tank and flows into the drainage pond 8. The flow of water at this time is indicated by an arrow 17.
またろ過池4の洗浄時は洗浄水がろ過池4に保
給され、洗浄排水は矢印16の経路で排水池8へ
流入する。 Further, when cleaning the filter basin 4, the cleaning water is stored in the filter basin 4, and the cleaning waste water flows into the drainage basin 8 along the path indicated by the arrow 16.
排水池8に流入した水は返送流量制御装置20
で制御される返送ポンプ9および流量波節弁10
を介して着水井2に返送され、再利用される。な
お11は流量計である。 The water flowing into the drainage pond 8 is returned to the flow rate control device 20
A return pump 9 and a flow rate node valve 10 controlled by
The water is returned to the landing well 2 via the water receiving well 2 and reused. Note that 11 is a flow meter.
排水池8の水位hは洗浄時または排泥時に急激
に上昇するが、返送ポンプ9との流量調節弁10
を用いて排水池8の水位hを制御すると返送流量
Qbが増大し、結果として過大な排水が着水井2
に返送されて浄水の水質を低下させる。 The water level h in the drainage basin 8 rises rapidly during cleaning or mud removal, but the flow rate control valve 10 connected to the return pump 9
When the water level h of the drainage pond 8 is controlled using
Qb increases and as a result, excessive wastewater flows into the landing well 2.
water is sent back to the water, reducing the quality of purified water.
このため排水返送制御装置19を用いて排水池
への流入流量パターンと排水池容量とを考慮した
最適計画法によつて返送流量を計画的に制御し、
これによつて返送流量を可能な限り一定に保持す
ることが行われている。 For this reason, the return flow rate is systematically controlled using the wastewater return control device 19 using an optimal planning method that takes into account the inflow flow rate pattern to the drainage basin and the capacity of the drainage basin.
This ensures that the return flow rate is kept as constant as possible.
しかし最適計画法とフイードバツク制御とを組
合せると、最適な返送流量目標値Qrが階段状に
変化するので、返送流量も階段状に大きく変動
し、着水井の水質が大幅に変動するので、この場
合も処理水質に悪影響をあたえる。 However, when the optimal planning method and feedback control are combined, the optimal return flow rate target value Qr changes in a step-like manner, so the return flow rate also changes greatly in a step-like manner, and the water quality of the receiving well changes significantly. It also has a negative impact on the quality of treated water.
本発明は、排水池への流入流量パターンと排水
池の容量とを考慮して、計画的に排水返送を運用
するための望ましい排水返送目標値のスケジユー
ルを演算し、これによつて排水池の水位を許容範
囲に制限しながら適正な処理水質を得る浄水場の
排水返送流量制御装置を提供することを目的とし
ている。
The present invention takes into consideration the inflow flow rate pattern into the drainage basin and the capacity of the drainage basin, calculates a schedule of a desirable wastewater return target value for systematically operating wastewater return, and thereby The object of the present invention is to provide a wastewater return flow rate control device for a water purification plant that obtains appropriate quality of treated water while limiting the water level to an allowable range.
本発明は、ろ過池の洗浄排水または沈殿池の排
泥処理排水を排水池を経由して着水井に返送する
排水返送流量を上記排水量および排水池水位に応
じて制御する浄水場の排水返送流量制御装置にお
いて、排水池流入流量、排水池水位および洗浄周
期または排泥周期から一日の排水池流入流量パタ
ーンを推定する演算ロジツクと、上記流入流量推
定パターンに基づいて返送流量の変動を最小にす
る排水返送流量計画スケジユールを算出する演算
ロジツクと、上記返送流量計画スケジユールを排
水池水位を所定範囲に制限しながらスムージング
した排水返送流量目標パターンを算出する演算ロ
ジツクを備え、上記算出した排水返送流量目標パ
ターンに従つて排水返送流量を制御し、これによ
つて洗浄や排泥による排水池への流入流量の変動
にかかわらず、排水池の水位を許容範囲に保ちな
がら排送返送流量をなだらかに制御し、浄水処理
における水質の向上をはかつたものである。
The present invention provides a wastewater return flow rate for a water treatment plant that controls the wastewater return flow rate for returning cleaning wastewater from a filtration basin or sludge treatment wastewater from a settling basin to a receiving well via a drainage basin in accordance with the above-mentioned wastewater volume and the water level of the drainage basin. The control device includes calculation logic that estimates the daily drainage basin inflow flow rate pattern from the drainage basin inflow flow rate, drainage basin water level, and cleaning cycle or sludge cycle, and minimizes fluctuations in the return flow rate based on the above inflow flow rate estimation pattern. A calculation logic for calculating a wastewater return flow rate plan schedule to be calculated, and a calculation logic for calculating a target wastewater return flow rate pattern obtained by smoothing the return flow rate plan schedule while limiting the drainage pond water level within a predetermined range. The wastewater return flow rate is controlled according to the target pattern, and this allows the wastewater return flow rate to be smoothed out while maintaining the water level in the drainage pond within an acceptable range, regardless of fluctuations in the flow rate flowing into the drainage pond due to cleaning and sludge removal. control and improve water quality in water purification treatment.
本発明の一実施例を第1図に示す。 An embodiment of the present invention is shown in FIG.
第1図は本発明による排水返送流量制御装置の
演算動作を示すフローチヤートであり、排水池流
入流量Qt,排水池水位hの時系列データ、ろ過
池洗浄周期△T1,沈殿池排泥周期△T2および時
刻Tを入力して、計画作成周期ごとの排水返送流
量目標値Qrを算出する。 FIG. 1 is a flowchart showing the calculation operation of the wastewater return flow rate control device according to the present invention, which shows the time series data of the drainage basin inflow flow rate Qt, the drainage basin water level h, the filter cleaning cycle △T 1 , and the sedimentation basin sludge drainage cycle. By inputting ΔT 2 and time T, the wastewater return flow rate target value Qr for each plan creation cycle is calculated.
すなわちステツプ(1)で上記各プロセス値および
設定値を入力し、ステツプ(2)で1日分の排水池流
入水の1時間ごとの流量パターン推定量Q^t(k)
〔k=1〜24〕を算出する。 In other words, in step (1), each process value and set value are inputted, and in step (2), the estimated hourly flow rate pattern of one day's worth of inflow water to the drainage pond Q^t(k) is calculated.
Calculate [k=1 to 24].
次にステツプ(3)で排水返送流量計画スケジユー
ルQr*(k)〔k=1〜24〕を算出する。 Next, in step (3), a wastewater return flow rate planning schedule Qr * (k) [k=1 to 24] is calculated.
すなわち計画作成開始時刻の排水池水位から排
水池の貯排水量を求め、上記ステツプ(2)で求めた
排水池流入流量パターン推定値Q^t(k)と排水池容
量とから望ましい排水返送流量計画スケジユール
Qr*(k)を算出する。 In other words, the storage volume of the drainage pond is determined from the drainage pond water level at the time when the plan creation starts, and the desired wastewater return flow rate plan is calculated from the estimated value Q^t(k) of the drainage basin inflow flow rate pattern obtained in step (2) above and the drainage basin capacity. schedule
Calculate Qr * (k).
上記排水返送流量計画スケジユールQ*r(k)の
演算は、排水返送流量の変動を最小化する最小化
問題として下記のように定式化される。 The calculation of the wastewater return flow rate planning schedule Q * r(k) is formulated as follows as a minimization problem that minimizes fluctuations in the wastewater return flow rate.
目的関数;24
〓k=1
(I・x(k)2→最小 …(1)
制約条件; |x(k)|<Cx …(2)
fn<Qr*(k)<fx (3)
Hn<H(k)<Hx …(4)
ここに Q^*(k)=F.y(k)
y(k)=y(k-1)x(k)
y(o),H(o):所定値
H(k)=Qt(k)−Qr*(k)/A+H(k-1)
また x=(x1,x2,…,xd)
y=(y1,y2,…,yd)
xi,yi=0または1(i=1〜d)
F=(f1,f2,…,fd)
fi;排水返送流量変更値(i=1〜d)
Cx;0または正の整数でxのノルムの上
限
fx,fm;排水返送流量の上下限値
Hx,Hm;排水池水位の上下限値
I;単位行列
A;排水池断面積
H(k);時間帯kの排水池水位
Qr*(k);時間帯kの排水返送流量計画値
Q^t(k);時間帯kの排水池流入流量推定値
上式のように0−1整数計画問題として定式化
し、分岐限定法を用いて、次の1日分の排水返送
流量計画スケジユールQr*(k)〔k=1〜24〕を算
出する。 Objective function; 24 〓 k=1 (I・x(k) 2 → minimum …(1) Constraints; |x(k)|<Cx …(2) fn<Qr * (k)<fx (3) Hn <H(k)<Hx …(4) Here Q^ * (k)=Fy(k) y(k)=y(k -1 )x(k) y(o), H(o): Predetermined Value H(k)=Qt(k)−Qr * (k)/A+H(k -1 ) Also, x=(x 1 , x 2 ,…, xd) y=(y 1 , y 2 ,…, yd) xi, yi = 0 or 1 (i = 1 to d) F = (f 1 , f 2 , ..., fd) fi; Drainage return flow rate change value (i = 1 to d) Cx; 0 or a positive integer x upper limit of norm fx, fm; upper and lower limits of wastewater return flow rate Hx, Hm; upper and lower limits of drainage pond water level I; unit matrix A; drainage basin cross-sectional area H(k); drainage basin water level in time period k Qr * (k); Planned value of wastewater return flow rate for time period k Q^t(k); Estimated value of drainage pond inflow flow rate for time period k Formulated as a 0-1 integer programming problem as shown in the above equation, and using the branch and bound method. Then, calculate the wastewater return flow rate plan schedule Qr * (k) [k=1 to 24] for the next day.
次にステツプ(4)でスムージングを行う。すなわ
ちステツプ(3)で求めた計画スケジユールQr*が時
間帯が変るごとに不連続な変化をするので、これ
らを連続的な計画目標パターンQr′(t)〔t=t1
〜t24〕に変換する。 Next, smoothing is performed in step (4). In other words, since the planned schedule Qr * obtained in step (3) changes discontinuously as the time period changes, these can be combined into a continuous planned target pattern Qr'(t) [t=t 1
~ t24 ].
このため、先ず計画スケジユールQr*に従つて
排水返送を行つたとしたときの各時間帯kでの排
水池水位h*(k)を下記(5)式を用いて推定する。 For this reason, first, assuming that the wastewater is returned according to the planned schedule Qr * , the water level h * (k) of the drainage pond in each time period k is estimated using the following equation (5).
h*(k)=Qt(k)−Qr*(k)/A+h*(k−1) …(5)
この場合計画作成開始時の排水池水位はh*
(o)である。 h * (k)=Qt(k)−Qr * (k)/A+h * (k−1) …(5) In this case, the drainage pond water level at the start of planning is h *
(o).
一般に排水返送流量計画値は時刻k(時間帯k
の終了時点)にQr*(k)からQr*(k+1)にステツ
プ状に変化するが、時刻k−Tから時刻k+Tま
で時間2T間にQr*(k)からQr*(k+1)へ直線状
の傾斜で下記(6)式
Qr′(t)=Qr*(k+1)−Qr*(k)/2T・t+Qr*(
k)
…(6)
ここにt;時刻k−Tからの経過時間に示す
Qr′(t)で変化させたと仮定すると、排水池の水
位推定値k′(t)は下記(7)式であたえられる。 Generally, the wastewater return flow rate planned value is calculated at time k (time period k
Qr * (k) changes stepwise to Qr * (k+1) at the end of the period), but it changes linearly from Qr * (k) to Qr * (k+1) in 2T from time k-T to time k+T. With the slope of
k) …(6) Here t; Shows the elapsed time from time k-T.
Assuming that the water level is changed by Qr'(t), the estimated water level of the drainage pond k'(t) is given by the following equation (7).
h′=Qrk*/A(t−t2/4T)+H0−Qrk*/A・T…(7)
ここに Qrk*=Qr*(k+1)−Qr*(k)
スムージングに際しては、水位変動が所定値以
下になるよう、すなわち次の(8)式が成立するよう
にパラメータTを選定する。h'=Qrk * /A (t-t 2 /4T) + H 0 -Qrk * /A・T...(7) Here, Qrk * = Qr * (k+ 1 ) - Qr * (k) When smoothing, the water level The parameter T is selected so that the fluctuation is below a predetermined value, that is, so that the following equation (8) holds true.
hHWL<h′(t)<hLWL …(8)
ここに kHWL;排水池水位上限
kLWL;排水池水位下限
これによつてスムージングしたなめらかな排水
流量計画目標パタンQr′(t)〔t=t1,t2,…,
t24〕が算定される。 h HWL <h′(t)<h LWL …(8) Here k HWL ; Upper limit of drainage pond water level k LWL ; Lower limit of drainage pond water level This smoothes the drainage flow rate planning target pattern Qr′(t) [ t=t 1 , t 2 ,...,
t 24 ] is calculated.
次にステツプ(5)で実際のプロセス値すなわち返
送流量Qbおよび排水池水位hを入力し、ステツ
プ(6)で上記排水流量計画目標パターンQr′(t)に
フイードバツク補正を加えて返送流量目標パター
ンQr(t)を算出し、これを目標値として返送流
量Qbを制御する。 Next, in step (5), the actual process values, that is, the return flow rate Qb and the drainage pond water level h are input, and in step (6), feedback correction is added to the drainage flow rate planning target pattern Qr'(t) to create the return flow rate target pattern. Qr(t) is calculated and the return flow rate Qb is controlled using this as a target value.
これによつて返送流量の急激な変動を抑制しな
がら適正な排水返送制御を行うことが可能とな
る。 This makes it possible to perform appropriate drainage return control while suppressing rapid fluctuations in the return flow rate.
上記実施例では、排水池への流入流量パターン
の推定に洗浄周期および排泥周期を用いたが、排
泥処理排水を着水井に返送しない場合は、洗浄周
期だけを入力すればよい。 In the above embodiment, the cleaning cycle and the sludge cycle are used to estimate the inflow flow rate pattern to the drainage pond, but if the sludge treated wastewater is not to be returned to the landing well, only the cleaning cycle may be input.
また洗浄水を着水井に返送しない場合は、排泥
周期だけを入力すればよい。 Furthermore, if the wash water is not to be returned to the receiving well, only the sludge removal period needs to be input.
また洗浄または排泥が一定周期で行われない場
合には、洗浄周期または排泥周期の代りに、洗浄
または排泥のスケジユールを入力すればよい。 Furthermore, if cleaning or mud removal is not performed at regular intervals, a cleaning or mud removal schedule may be input instead of the cleaning cycle or mud removal cycle.
また上記実施例では、(6)式の関数形として排水
返送流量計目標パターンQr′(t)を時間tの一次
式として与えたが、時間tの多項式として与える
ことも可能であり、他の関数形を用いることも可
能である。 Further, in the above embodiment, the target pattern Qr'(t) of the wastewater return flowmeter is given as a linear expression of time t as a function form of equation (6), but it is also possible to give it as a polynomial of time t. It is also possible to use functional forms.
以上説明したように本発明によれば、ろ過池洗
浄または沈殿池排泥によつて排水が一時的に増大
しても、着水井への返送流量の変動を排水池の水
位変動の許す範囲でなめらかにし、これによつて
処理水質を安定化できる合理的な浄水場の排水返
送流量制御装置が得られる。
As explained above, according to the present invention, even if the drainage volume temporarily increases due to filter cleaning or sedimentation tank drainage, fluctuations in the flow rate returned to the receiving well can be controlled within the range permitted by the water level fluctuations in the drainage basin. A rational wastewater return flow rate control device for a water treatment plant that can stabilize the quality of treated water can be obtained.
第1図は本発明の一実施例を示すフローチヤー
ト、第2図は浄水場の一般的なプロセス構成を示
す系統図である。
1……原水、2……着水井、3……沈殿池、4
……ろ過池、5……浄水池、8……排水池、9…
…返送ポンプ、10……流量調節弁、19……排
水返送制御装置、20……返送流量制御装置。
FIG. 1 is a flowchart showing one embodiment of the present invention, and FIG. 2 is a system diagram showing a general process configuration of a water purification plant. 1... Raw water, 2... Landing well, 3... Sedimentation pond, 4
...Filtration pond, 5...Water purification pond, 8...Drainage pond, 9...
...Return pump, 10...Flow rate control valve, 19...Drainage return control device, 20...Return flow rate control device.
Claims (1)
水を排水池を経由して着水井に返送する排水返送
流量を上記排水量および排水池水位に応じて制御
する浄水場の排水返送流量制御装置において、排
水池流入流量、排水池水位および洗浄周期または
排泥周期から一日の排水池流入流量パターンを推
定する演算ロジツクと、上記流入流量推定パター
ンに基づいて返送流量の変動を最小にする排水返
送流量計画スケジユールを算出する演算ロジツク
と、上記返送流量計画スケジユールを排水池水位
を所定範囲に制限しながらスムージングした排水
返送流量目標パターンを算出する演算ロジツクを
備え、上記算出した排水返送流量目標パターンに
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。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 or sludge treatment wastewater from a sedimentation basin and returning it to a receiving well via a drainage basin in accordance with the above-mentioned quantity of wastewater and the water level of the drainage basin. , calculation logic that estimates the daily drainage basin inflow flow rate pattern from the drainage basin inflow flow rate, drainage basin water level, and cleaning cycle or sludge cycle, and wastewater return that minimizes fluctuations in the return flow rate based on the above inflow flow rate estimation pattern. A calculation logic that calculates a flow rate planning schedule, and a calculation logic that calculates a wastewater return flow rate target pattern obtained by smoothing the return flow rate plan schedule while limiting the drainage pond water level within a predetermined range, Therefore, a wastewater return flow rate control device for a water purification plant is characterized in that it controls the wastewater return flow rate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23244884A JPS61111186A (en) | 1984-11-06 | 1984-11-06 | Device for controlling flow rate of return waste water in water purifying plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23244884A JPS61111186A (en) | 1984-11-06 | 1984-11-06 | Device for controlling flow rate of return waste water in water purifying plant |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61111186A JPS61111186A (en) | 1986-05-29 |
| JPH025152B2 true JPH025152B2 (en) | 1990-01-31 |
Family
ID=16939436
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP23244884A Granted JPS61111186A (en) | 1984-11-06 | 1984-11-06 | Device for controlling flow rate of return waste water in water purifying plant |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61111186A (en) |
-
1984
- 1984-11-06 JP JP23244884A patent/JPS61111186A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61111186A (en) | 1986-05-29 |
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