JPS5952449B2 - Filtration flow control device - Google Patents
Filtration flow control deviceInfo
- Publication number
- JPS5952449B2 JPS5952449B2 JP54099490A JP9949079A JPS5952449B2 JP S5952449 B2 JPS5952449 B2 JP S5952449B2 JP 54099490 A JP54099490 A JP 54099490A JP 9949079 A JP9949079 A JP 9949079A JP S5952449 B2 JPS5952449 B2 JP S5952449B2
- Authority
- JP
- Japan
- Prior art keywords
- flow rate
- water level
- filtration
- raw water
- value
- 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
Landscapes
- Control Of Non-Electrical Variables (AREA)
- Filtration Of Liquid (AREA)
- Flow Control (AREA)
Description
【発明の詳細な説明】
この発明は、浄水場の濾過段階における濾過流量制御装
置に関するものであり、更に詳しくは、原水の取水流量
の変更があつたとき、或いは外乱要因が発生したとき、
前記制御装置における濾過流量設定値を如何に変更・修
正するかという設定値の適切な決定方式に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a filtration flow rate control device in the filtration stage of a water purification plant, and more specifically, when the intake flow rate of raw water is changed or when a disturbance factor occurs,
The present invention relates to an appropriate method for determining a set value of how to change or correct the filtration flow rate set value in the control device.
第1図は、浄水プロセスの概要とこの発明の一実施例を
示す概要図であるが、先ず第1図における浄水プロセス
の概要を参照して従来技術の問題点を説明する。FIG. 1 is a schematic diagram showing an overview of a water purification process and an embodiment of the present invention. First, problems of the prior art will be explained with reference to the overview of the water purification process in FIG.
一般に浄水プロセスは、第1図にみられるように、河川
等から取水した原水を沈砂池1に導き、水と共に流入す
る土砂、礫等を沈澱除去し、次に沈澱池2において水中
の浮遊物、微細な粒子等を沈澱させ、その後、一旦水を
濾過池原水渠3に貯jえてから濾過池4へ送り、堆砂層
を通過させて濾過した後、混和池5、浄水池6を経て送
水するものであり、取水から送水まで数時間にも及ぶと
いう長時間を要するプロセスである。Generally, in the water purification process, as shown in Figure 1, raw water taken from a river, etc. is led to a settling tank 1, where sediment, gravel, etc. that flow in with the water are removed by sedimentation, and then in a settling tank 2, suspended matter in the water is removed. , fine particles, etc. are precipitated, and then the water is temporarily stored in the filtration basin raw water conduit 3 and then sent to the filtration basin 4, where it is passed through a sediment layer and filtered, and then sent through the mixing basin 5 and the water purification basin 6. It is a long process that takes several hours from water intake to water delivery.
そして浄水場では、一般に或る水需要パターンまたは取
水量制、限等により、適当な時間帯毎に、原水の取水流
量を変更するという運用方式が採られている。他方、浄
水場からの送水流量の制御は、濾過池4からの濾過流量
の制御によつて行なわれる。しかし、原水の取水流量が
変化しても、その影響が濾過池4にまで及ぶには相当の
時間遅れを伴うから、取水流量の変更と同時に濾過流量
制御における設定値を変更するようなことは出来ない。
取水流量の変更があつた場合、それに対する最適な濾過
流量設定値の決定は、浄水ブラント保全の立場から原水
渠3の水位を一定の変動幅の範囲内に保つこと、水質の
安定を図る立場から濾過池における濾過流量の変動を極
力少なくすること、濾過流量を濾過能力の範囲内で最大
限まで変化させて広い運用性を実現すること等を条件と
して行なうのがよい。さて、従来、上述の如き最適な濾
過流量設定値の決定方式としては、取水された原水流量
、濾過池原水渠の水位およびその変動状況、浄水池の水
位およびその変動状況等を監視し、それら各データに基
づき所定の演算を行ない、演算結果により濾過流量設定
値を遂次変更する方式が知られている。In water purification plants, an operation method is generally adopted in which the intake flow rate of raw water is changed at appropriate time periods depending on a certain water demand pattern or water intake amount restrictions. On the other hand, the flow rate of water sent from the water purification plant is controlled by controlling the flow rate of filtration from the filter basin 4. However, even if the raw water intake flow rate changes, there is a considerable time delay before the effect reaches the filtration basin 4, so it is not recommended to change the set value for filtration flow rate control at the same time as the water intake flow rate is changed. Can not.
When there is a change in water intake flow rate, determining the optimal filtration flow rate setting value should be determined from the standpoint of water purification brand maintenance by maintaining the water level in raw water culvert 3 within a certain range of fluctuation, and from the standpoint of stabilizing water quality. It is preferable to do this under conditions such as minimizing fluctuations in the filtration flow rate in the filtration pond, and varying the filtration flow rate to the maximum extent within the range of the filtration capacity to achieve a wide range of operability. Conventionally, as a method for determining the optimum filtration flow rate setting value as described above, the flow rate of raw water taken, the water level of the filtration pond raw water conduit and its fluctuations, the water level of the water purification pond and its fluctuations, etc. are monitored, and each of these is monitored. A method is known in which a predetermined calculation is performed based on data and the filtration flow rate set value is successively changed based on the calculation result.
しかし、従来のかかる方式は、データの演算機構が複雑
であること、濾過流量設定値が逐次変更されるため、濾
過流量の制御頻度が高いこと、連続濾過プロセスを前提
としたものであるため、取水の停止・開始を行なう際に
は適用が困難であること、等の問題点があつた。この発
明は、上述の如き従来技術の問題点を解決するためにな
されたもであり、従つてこの発明の目的は、必要なデー
タ演算機構が簡便化されたものであり、1回の取水量変
更に対し何度も逐次的に設定値を変更する必要がなく、
その上、通常運転時は勿論のこと、取水の開始・停止時
においても適用可能であり、かつ外乱要因の発生に対応
可能な最適濾過流量設定値決定方式を備えた濾過流量制
御装置を提供することにある。However, such a conventional method has a complicated data calculation mechanism, the filtration flow rate setting value is changed sequentially, so the filtration flow rate has to be controlled frequently, and it is based on the premise of a continuous filtration process. There were problems such as difficulty in applying it when stopping and starting water intake. This invention was made in order to solve the problems of the prior art as described above, and therefore, the purpose of this invention is to simplify the necessary data calculation mechanism and reduce the amount of water taken per time. There is no need to sequentially change the setting value over and over again in response to changes.
Furthermore, the present invention provides a filtration flow rate control device that is applicable not only during normal operation but also when starting and stopping water intake, and is equipped with an optimal filtration flow rate setting value determination method that can cope with the occurrence of disturbance factors. There is a particular thing.
この発明の構成の要点は、前記設定値を、プロセスへの
原水の設定された流入量と、濾過池へ流入する原水をそ
の前に一旦貯水する原水渠の水位の、該渠における或る
設定水位上限値および下限値に対する相対的レベル位置
と、原水渠における水位の変化傾向とに依存して決定す
るように構成した点にある。The main point of the configuration of this invention is that the set value is determined by a set inflow rate of raw water into the process and a certain setting of the water level of the raw water conduit where the raw water flowing into the filtration pond is temporarily stored beforehand. The point is that the determination is made depending on the relative level position with respect to the upper and lower limits of the water level and the change tendency of the water level in the raw water culvert.
次に、再び第1図を参照してこの発明の一実施例を詳細
に説明する。Next, referring again to FIG. 1, one embodiment of the present invention will be described in detail.
なお、先ほどの浄水プロセスの概要説明のときには説明
しなかつたが、濾過ノ池原水渠3から混和池5に至る間
に、濾過池4は1個ではなく複数個並列に、プロツク7
・・・・・・・・・・・・・・・7″の如く設けられて
いるのが普通であり、この発明において問題とする濾過
流量は、各濾過池全部の総濾過流量である。Although it was not explained earlier when explaining the outline of the water purification process, between the filtration pond raw water conduit 3 and the mixing basin 5, there is not one filtration basin 4 but multiple filtration basins in parallel, and the process 7
7'' is normally provided, and the filtration flow rate of interest in this invention is the total filtration flow rate of all the filter basins.
第1図において、原水流量設定値発生器8と、原水流量
制御装置9と、原水流量計10と、原水流量調節弁11
と、により原水の取水量調節系が構成されている。In FIG. 1, a raw water flow rate set value generator 8, a raw water flow rate control device 9, a raw water flow meter 10, a raw water flow rate control valve 11
A raw water intake control system is constructed by the following.
そのほか、沈砂池1と沈澱池2における損失流量分の信
号を発生する損失流量発生器13を含む総濾過流量目標
値発生器12と、総濾過流量設定値発生器14と、濾過
池原水渠水位計15と、濾過流量制御装置16と、濾過
流量調節弁17と、濾過流量計18と、浄水弁19と、
濾過流量加算器20と、が図示の如く接続されている。
次に動作を説明する。In addition, a total filtration flow rate target value generator 12 including a loss flow rate generator 13 that generates a signal for the loss flow rate in the settling basin 1 and settling basin 2, a total filtration flow rate set value generator 14, and a filtration basin raw water conduit water level gauge. 15, a filtration flow rate control device 16, a filtration flow rate adjustment valve 17, a filtration flowmeter 18, a water purification valve 19,
A filtration flow rate adder 20 is connected as shown.
Next, the operation will be explained.
原水流量設定値発生器8は、或る取水計画のパターンに
従い原水流量設定値GSを出力する。原水流量制御装置
9は、原水流量計10よりの入力である原水流量GQと
、原水流量設定値発生器8より与えられた原水流量設定
値GSが等しくなるように原水流量調節弁11を制御す
る。また原水流量制御装置9は、その制御モードにより
、つまり自動モードのときは原水流量設定値GSを、ま
た手動モードのときは原水流量GQを総濾過流量目標値
発生器12に対して出力する。該発生器12では、制御
装置9の出力である原水流量設定値GSまたは原水流量
GQから、沈砂池1および沈澱池2における損失流量分
(損失流量発生器13から発生)を減じたものを、総濾
過流量目標値RGとして総濾過流量設定値発生器14へ
与える。該発生器14では、時間△t(原水渠3の水位
監視周期)ごとに、濾過池原水渠水位計15からの水位
Hと、原水渠3における水位設定値上限GHと、同下限
GLと、総濾過流量目標値RGとの関係から、演算によ
つて総濾過流量設定値RSを求め、濾過流量制御装置1
6に対して出力する。すなわち、H(原水渠3の水位)
の監視周期△t毎に、HがGHより大きく、RGがRS
より大きいとき (H>GH.RG〉RS)、またはH
がGLより小さく、RGがRSより小さいとき(H<G
L.RG<RS)、RS=RGとなるようにRS(総濾
過流量設定値)を更新するのである。さらに、原水渠3
における水位が外乱要因の発生により、所定の水位変動
幅(上限GHと下限GLの間)を逸脱した場合、上記の
如き、総濾過流量設定値RSの更新方式を採用している
だけでは、総濾過流量目標値RGが一定であるので、原
水渠3における水位の復元は不可能である。The raw water flow rate set value generator 8 outputs a raw water flow rate set value GS according to a pattern of a certain water intake plan. The raw water flow rate control device 9 controls the raw water flow rate control valve 11 so that the raw water flow rate GQ input from the raw water flow meter 10 and the raw water flow rate set value GS given from the raw water flow rate set value generator 8 are equal. . Further, the raw water flow rate control device 9 outputs the raw water flow rate set value GS in the automatic mode, and the raw water flow rate GQ in the manual mode to the total filtration flow rate target value generator 12 depending on the control mode. In the generator 12, the raw water flow rate set value GS or the raw water flow rate GQ, which is the output of the control device 9, is calculated by subtracting the loss flow rate in the settling basin 1 and the settling basin 2 (generated from the loss flow rate generator 13). It is given to the total filtration flow rate set value generator 14 as the total filtration flow rate target value RG. The generator 14 outputs the water level H from the filtration basin raw water conduit water level meter 15, the upper limit GH of the water level set value in the raw water conduit 3, the lower limit GL of the water level, and the total Based on the relationship with the filtration flow rate target value RG, the total filtration flow rate setting value RS is determined by calculation, and the filtration flow rate control device 1
Output for 6. In other words, H (water level of raw water channel 3)
At every monitoring period Δt, H is greater than GH and RG is RS
When larger than (H>GH.RG>RS), or H
is smaller than GL and RG is smaller than RS (H<G
L. RS (total filtration flow rate set value) is updated so that RG<RS) and RS=RG. In addition, raw water channel 3
If the water level at deviates from the predetermined water level fluctuation range (between the upper limit GH and lower limit GL) due to the occurrence of a disturbance factor, simply adopting the method of updating the total filtration flow rate set value RS as described above will not result in the total Since the filtration flow rate target value RG is constant, it is impossible to restore the water level in the raw water culvert 3.
そこで、この発明では、この点にも考慮を払つている。
以下詳しく説明する。原水渠3の水位を変化させる外乱
要因としては、濾過池4の洗浄終了後の充水が挙げられ
る。Therefore, the present invention takes this point into consideration.
This will be explained in detail below. A disturbance factor that changes the water level of the raw water conduit 3 is the filling of the filter basin 4 with water after cleaning is completed.
先にも述べたが、濾過池4は複数個あり、適当に交替で
各池の掃除がなされるものであり、そのような洗浄終了
後の当該池への充水により原水渠3の水位は急激に降下
する。そのほかの外乱要因としては、各種設定値の不適
切さが挙げられる。つまり水位監視周期△t、上下限の
設定値GH、GL、総濾過流量目標値RG等が不適切で
あると、原水渠の水位は上昇または下降して所定の変動
幅を逸脱するし、オペレータの手動操作等による濾過流
量の変化によつても水位は上昇或いは下降して所定の変
動幅を逸脱することがある。そこで、このような場合、
水位の復元を図るため、総濾過流量設定値発生器14で
は、HがGHより大きいにもかかわらず、RGがRSに
等しいか小さく、Hが上昇傾向をたどつているとき(H
>GH.RGdHくRS、一〉0)、RSに対し増加方
向の補正を) Dt加える。As mentioned earlier, there are multiple filtration ponds 4, and each pond is cleaned in appropriate shifts, and after such cleaning is completed, the water level in the raw water culvert 3 is reduced by filling the pond with water. descend rapidly. Other disturbance factors include inappropriateness of various setting values. In other words, if the water level monitoring cycle △t, the upper and lower limit set values GH and GL, and the total filtration flow rate target value RG, etc. are inappropriate, the water level in the raw water channel will rise or fall and deviate from the predetermined fluctuation range, and the operator Due to a change in the filtration flow rate due to manual operation or the like, the water level may rise or fall and deviate from a predetermined fluctuation range. Therefore, in such a case,
In order to restore the water level, the total filtration flow rate set value generator 14 sets the value when RG is equal to or smaller than RS and H is following an upward trend (H
>GH. RGdH × RS, 1>0), add an increasing correction to RS) Dt.
つまり、RS(1+α)を新たなRSとする。但しRS
く(1+β)RGでなければならない。またHがGLよ
り小さいにもかかわらず、RGがRSに等しいか大きく
、Hが下降傾向をたどつているとき(H<GL.RG>
RS.立W〈0)) ) Dt)RSに対し減
少方向で補正を加える。In other words, RS(1+α) is set as a new RS. However, RS
(1+β)RG. Also, when H is smaller than GL, RG is equal to or larger than RS, and H is following a downward trend (H<GL.RG>
R.S. (W〈0)) ) Dt) Add correction to RS in the decreasing direction.
つまりRS(1−α)を新たなRSとする。但しRS〉
(1β)RGでなくてはならない。ここでα (1〉α
〉0)とβ (1〉β〉0)は、水位復元の速度に関す
る値であり、原水渠の容量、最大濾過能力、濾過池面積
等により決定される値である。濾過流量制御装置16は
、複数個存在する各濾過池4への濾過流量設定値配分を
行ない、一池毎の濾過流量設定値Rsを求め、濾過流量
計18よりの入力であるRq(濾過流量)とRsが等し
くなるように、浄水弁19の開閉による濾過の開始およ
び停止、または濾過流量調節弁17の操作による調節を
行なう制御ループと、濾過流量加算器20の出力である
RQ(各濾過池4における濾過流量の合計)とRSを監
視する制御ループより構成される。次に、外乱要因発生
に対し、この発明により設定値を修正する場合について
、総濾過流量目標値RG、濾過池原水渠水位H、総濾過
流量設定値RS、総濾過流量RQの時間的変化を、第2
図乃至第5図を参照して説明する。第2図乃至第5図に
共通な全時間帯においては、原水流量は一定とし、その
結果、総濾過流量目標値RG(第2図)は一定値を示す
。In other words, RS(1-α) is set as a new RS. However, RS>
(1β) Must be RG. Here α (1〉α
〉0) and β (1〉β〉0) are values related to the speed of water level restoration, and are determined by the capacity of the raw water conduit, the maximum filtration capacity, the area of the filter pond, etc. The filtration flow rate control device 16 allocates the filtration flow rate setting value to each of the plurality of filtration ponds 4, obtains the filtration flow rate setting value Rs for each pond, and calculates the filtration flow rate setting value Rs, which is the input from the filtration flow meter 18 (Rq (filtration flow rate) ) and Rs are equal to each other. It consists of a control loop that monitors the total filtration flow rate in the pond 4) and RS. Next, regarding the case where the set values are corrected according to the present invention in response to the occurrence of a disturbance factor, the temporal changes in the total filtration flow rate target value RG, the filtration pond raw water level H, the total filtration flow rate set value RS, and the total filtration flow rate RQ are as follows. Second
This will be explained with reference to FIGS. 5 to 5. In all the time periods common to FIGS. 2 to 5, the raw water flow rate is constant, and as a result, the total filtration flow rate target value RG (FIG. 2) shows a constant value.
時刻ち以前は、濾過池原水渠水位(第3図)は安定した
水位状態にあり、従つてRG=RSである。今時刻ちに
おいて、濾過池洗浄終了に伴う濾過池充水が行なわれた
とすると、第3図A点にみられるように、原水渠水位H
は急激に低下する。時刻t1では、HはGLよりも低く
、RG:RSでかつHは下降傾向にあるので、総濾過流
量設定値発生器14では、濾過流量制御装置16に対す
る総濾過流量設定値RSの補正を減少方向で行なう。す
なわち、時刻t1における設定値RS(t1)は、時刻
ちにおける設定値RS(TO)の(1−α)倍とする。
式で表現するとRS(t1)=RS(TO)・ 〔1−
α〕くRG(TO)=RG(t1)。時刻T2において
も、同様の条件にあるため設定値RSの補正を行なう。
すなわちRG(TO)・ 〔1−β〕〈RS(T2)=
RS(t1)・ 〔1−α〕=RS(TO)・ 〔1−
α〕2くRG(TO)=RG(t1)=RG(T2)。
時刻T3においては、HはGLよりも低く、RSもRG
より小さいが、Hは上昇傾向にある(水位が復元方向に
向かつていフる)ため、設定値RSの補正は行なわず、
RS(T3)=RS(T2)である。水位Hが徐々に上
昇してゆき時刻T4においてはHはGHより高く、RG
がRS〔=RS(T2)=RS(t1)〕よりも大きい
ので、総濾過流量設定値発生器14では、RG=RS7
〔=RG(TO)〕となるように設定値RSの変更を行
なう。次に、原水の取水量を或る時間帯ごとに変化させ
るという通常の運用方式を採つたときの、原水流量設定
値GS、原水流量GQ、濾過流量目標値′)RG、原水
渠における水位H、総濾過流量設定値RS、総濾過流量
RQの時間的変化を、第6図乃至第11図を参照して説
明する。Before time 1, the filtration pond raw water level (Fig. 3) is in a stable water level state, and therefore RG=RS. Assuming that the filtration pond has been filled with water due to the completion of filtration cleaning, the water level of the raw water channel H
decreases rapidly. At time t1, H is lower than GL, RG:RS, and H is on a downward trend, so the total filtration flow rate set value generator 14 reduces the correction of the total filtration flow rate set value RS to the filtration flow rate controller 16. Do it in the direction. That is, the set value RS(t1) at time t1 is set to (1-α) times the set value RS(TO) at time t.
Expressed as a formula, RS(t1)=RS(TO)・[1-
α] RG(TO)=RG(t1). At time T2, since the same conditions exist, the set value RS is corrected.
That is, RG(TO)・[1−β]〈RS(T2)=
RS(t1)・[1-α]=RS(TO)・[1-
α]2 RG (TO) = RG (t1) = RG (T2).
At time T3, H is lower than GL, and RS is also lower than RG.
Although it is smaller, H is on the rise (the water level is moving in the direction of restoration), so the set value RS is not corrected.
RS(T3)=RS(T2). The water level H gradually rises, and at time T4, H is higher than GH, and RG
is larger than RS [=RS(T2)=RS(t1)], so in the total filtration flow rate set value generator 14, RG=RS7
The set value RS is changed so that [=RG(TO)]. Next, when a normal operation method is adopted in which the raw water intake amount is changed every certain time period, the raw water flow rate setting value GS, raw water flow rate GQ, filtration flow rate target value ')RG, and water level H in the raw water channel are calculated. , the total filtration flow rate set value RS, and the total filtration flow rate RQ over time will be explained with reference to FIGS. 6 to 11.
今時刻T5で原水流量設定値GSの変更が行なわれたと
すると、原水流量GQがそれに追従すると共に、濾過流
量目標値RGも追従し、RG(T5)が設定される。If the raw water flow rate set value GS is changed at current time T5, the raw water flow rate GQ follows it, and the filtration flow rate target value RG also follows, and RG (T5) is set.
RSの設定変更が行なわれるのは、原水流量GQの増加
に伴い、HがGH以上となる時刻T6においてである。
同様に時刻T7で原水流量を減少させた場合、RSの設
定変更が行なわれるのは、原水流量減少に伴いHがGL
より低くなる時刻T8においてである。再び時刻T9に
おいて原水流量を増加させたとき、RSの設定変更は時
刻TlOにおいて行なわれる。第12図乃至第17図は
、時刻Tllにおいて取水の停止動作に入り、時刻Tl
7で濾過流量RQが零となるまでの経過を、GS.GQ
.RG.H.RS、RQのそれぞれについて示した時間
的変化図である。The setting of RS is changed at time T6 when H becomes equal to or higher than GH as the raw water flow rate GQ increases.
Similarly, when the raw water flow rate is decreased at time T7, the setting of RS is changed because H changes to GL as the raw water flow rate decreases.
This is at time T8 when the value becomes lower. When the raw water flow rate is increased again at time T9, the setting of RS is changed at time TlO. In FIGS. 12 to 17, water intake stops at time Tll, and water intake stops at time Tll.
7, the progress until the filtration flow rate RQ becomes zero is shown in GS.7. GQ
.. R.G. H. It is a time change diagram shown about each of RS and RQ.
以上説明した通りであるからこの発明によれば、濾過流
量制御装置における設定値の決定において、そのための
演算機構が比較的簡便であること、1回の取水量変更に
対する設定値の逐次的な何回にもわたる変更が不要なこ
と、通常運転時は勿論のこと取水の開始・停止時にも適
用可能であSること等の利点のほか、原水渠水位が、外
乱のため、または設定水位の上下限設定値、水位監視周
期が不適当であつたため、上下限設定範囲を逸脱した場
合にも、それを復元できるという利点がある。As explained above, according to the present invention, in determining the set value in the filtration flow rate control device, the calculation mechanism for this purpose is relatively simple, and the set value can be successively changed with respect to one change in water intake amount. In addition to the advantages that it does not require repeated changes and can be applied not only during normal operation but also when starting and stopping water intake, the raw water level may change due to disturbance or below the set water level. There is an advantage that even if the upper and lower limit set values and the water level monitoring cycle are inappropriate and deviate from the upper and lower limit set ranges, they can be restored.
第1図は、浄水プロセスの概要とこの発明の一実施例を
示す概要図、第2図乃至第5図は、それぞれ総濾過流量
目標値RG、濾過池原水渠水位H、総濾過流量設定値R
S、総濾過流量RQの時間的変化の一例を対応的に示す
タイムチヤートであり、第6図乃至第11図は、同様に
原水流量設定値GS、原水流量(1)、それにRG.H
.RS.RQのそれぞれの時間的変化の一例を対応的に
示すタイムチヤートであり、第12図乃至第17図は、
同様にGS.GQ.RG.H.RSおよびRQのそれぞ
れの時間的変化の一例を対応的に示すタイムチヤートで
ある。
図において、1は沈砂池、2は沈澱池、3は濾過池原水
渠、4は濾過池、5は混和池、6は浄水池、7は濾過池
4を含むプロツク、8は原水流量設定値発生器、9は原
水流量制御装置、10は原水流量計、11は原水流量調
節弁、12は総濾過流量目標値発生器、13は損失流量
発生器、14は総濾過流量設定値発生器、15は濾過池
原水渠水位計、16は濾過流量制御装置、17は濾過流
量調節弁、18は濾過流量計、19は浄水弁、20は濾
過流量加算器、を示す。Fig. 1 is a schematic diagram showing an overview of the water purification process and an embodiment of the present invention, and Figs. 2 to 5 show the total filtration flow rate target value RG, the filtration pond raw water channel water level H, and the total filtration flow rate set value R, respectively.
S is a time chart correspondingly showing an example of a temporal change in the total filtration flow rate RQ, and FIGS. 6 to 11 similarly show the raw water flow rate set value GS, raw water flow rate (1), and RG. H
.. R.S. FIGS. 12 to 17 are time charts showing examples of respective temporal changes in RQ, and FIGS.
Similarly, G.S. GQ. R.G. H. 3 is a time chart correspondingly showing an example of temporal changes in RS and RQ. In the figure, 1 is a settling basin, 2 is a sedimentation basin, 3 is a filtration basin, 4 is a filtration basin, 5 is a mixing basin, 6 is a water purification basin, 7 is a block including the filtration basin 4, and 8 is a raw water flow rate setting value generation. 9 is a raw water flow rate control device, 10 is a raw water flow meter, 11 is a raw water flow rate control valve, 12 is a total filtration flow rate target value generator, 13 is a loss flow rate generator, 14 is a total filtration flow rate set value generator, 15 16 is a filtration pond raw water channel water level gauge, 16 is a filtration flow rate control device, 17 is a filtration flow rate adjustment valve, 18 is a filtration flowmeter, 19 is a water purification valve, and 20 is a filtration flow rate adder.
Claims (1)
の濾過流量設定値RSに等しくなるように制御する濾過
流量制御装置において、濾過池へ流入する原水をその前
に一旦貯水する原水渠の水位Hが該渠における設定水位
上限値GHより高く、かつ原水の前記プロセスの設定さ
れた流入量に依存する濾過流量目標値RGが前記濾過流
量設定値RSより大なるとき、または前記水位Hが原水
渠における設定水位下限値GLより低く、かつ前記濾過
流量目標値RGが前記設定値RSより小なるとき、前記
濾過流量目標値RGと前記設定値RSが等しくなるよう
に、該設定値RSを更新すると共に、前記水位Hが前記
上限値GHより高いにかかわらず、前記目標値RGが前
記設定値RSに等しいか小さく、かつ前記水位Hが上昇
傾向にあるとき、前記設定値RSに対し増加方向の補正
を加え、また前記水位Hが前記下限値GLより低いにか
かわらず、前記目標値RGが前記設定値RSに等しいか
大きく、かつ前記水位Hが下降傾向にあるとき、前記設
定値RSに対し減少方向の補正を加えるようにして、前
記設定値RSが、プロセスへの原水の設定された流入量
と、濾過池へ流入する原水をその前に一旦貯水する原水
渠の水位の、該渠における或る設定水位上限値および下
限値に対する相対的レベル位置と、前記水位の変化傾向
とに依存して決定されるようにしたことを特徴とする濾
過流量制御装置。1 In a filtration flow rate control device that controls the filtration flow rate in a filtration pond in a water purification process to be equal to a predetermined filtration flow rate setting value RS, the water level H of a raw water culvert that temporarily stores raw water flowing into the filtration pond before it is is higher than the set water level upper limit GH in the culvert, and the filtration flow rate target value RG, which depends on the set inflow rate of the process of raw water, is greater than the filtration flow rate set value RS, or the water level H is higher than the set water level GH in the raw water culvert. When the set water level lower limit value GL is lower than the set water level lower limit value GL, and the filtration flow rate target value RG is smaller than the set value RS, the set value RS is updated so that the filtration flow rate target value RG and the set value RS become equal. At the same time, regardless of whether the water level H is higher than the upper limit value GH, when the target value RG is equal to or smaller than the set value RS, and the water level H is in an upward trend, the set value RS increases in an increasing direction. Regardless of whether the water level H is lower than the lower limit value GL, if the target value RG is equal to or larger than the set value RS, and the water level H is on a downward trend, In such a manner that the set value RS is corrected in the decreasing direction, the set value RS is calculated based on the set inflow rate of raw water to the process and the water level of the raw water conduit in which the raw water flowing into the filtration pond is temporarily stored beforehand in the conduit. 1. A filtration flow rate control device, characterized in that the flow rate control device is determined depending on a level position relative to a set upper limit value and lower limit value of the water level, and a change tendency of the water level.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54099490A JPS5952449B2 (en) | 1979-08-06 | 1979-08-06 | Filtration flow control device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54099490A JPS5952449B2 (en) | 1979-08-06 | 1979-08-06 | Filtration flow control device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5624611A JPS5624611A (en) | 1981-03-09 |
| JPS5952449B2 true JPS5952449B2 (en) | 1984-12-19 |
Family
ID=14248737
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP54099490A Expired JPS5952449B2 (en) | 1979-08-06 | 1979-08-06 | Filtration flow control device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5952449B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60174913U (en) * | 1984-04-25 | 1985-11-20 | 豊田合成株式会社 | Aquarium water level control device |
-
1979
- 1979-08-06 JP JP54099490A patent/JPS5952449B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5624611A (en) | 1981-03-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107544569A (en) | A kind of V-type filter state keeps the control method of constant level | |
| JPS5952449B2 (en) | Filtration flow control device | |
| CN104524844B (en) | For the liquid level controlling method of filter tank cleaning | |
| CN117090170B (en) | A control method and system for water distribution balance in open channels | |
| JP2008052508A (en) | Water treatment plant control system | |
| JPH0147237B2 (en) | ||
| JP3195863B2 (en) | Filter pond washing control device | |
| JPS5936060B2 (en) | Automatic inflow adjustment method for water distribution reservoirs and water purification reservoirs | |
| JP3577538B2 (en) | Method and apparatus for controlling flow rate of multiple filtration ponds in a water purification plant | |
| JPH05180169A (en) | Controller for water level in pump well | |
| JPS6313851Y2 (en) | ||
| JPS61182102A (en) | Controller for filtration plant | |
| JPH0468003B2 (en) | ||
| JPS5944643B2 (en) | How to operate a water supply system in a water supply system | |
| JP2921159B2 (en) | Filtration Pond Control Method by Fuzzy Inference | |
| RU1824447C (en) | Method for automatically controlling process of settling and vacuum-filtration of first-saturation juice in sugar production | |
| JPS583129Y2 (en) | "Filtration" cleaning control device for filtration pond | |
| JPH0123529Y2 (en) | ||
| JPS58159822A (en) | Controlling device of filter | |
| SU1286236A1 (en) | Automatic control system for liquid filter | |
| JP2001029937A (en) | Apparatus for controlling intake of water purification plant | |
| JPH03204701A (en) | Pump controller | |
| JPS61263688A (en) | Device for controlling use of water in water purification plant | |
| JPS63101905A (en) | Operation monitor and control equipment for filter plant | |
| JPS5886611A (en) | Flow rate controlling method |