JPS5840115A - Flocculant pouring control apparatus in water treatment - Google Patents
Flocculant pouring control apparatus in water treatmentInfo
- Publication number
- JPS5840115A JPS5840115A JP13989581A JP13989581A JPS5840115A JP S5840115 A JPS5840115 A JP S5840115A JP 13989581 A JP13989581 A JP 13989581A JP 13989581 A JP13989581 A JP 13989581A JP S5840115 A JPS5840115 A JP S5840115A
- Authority
- JP
- Japan
- Prior art keywords
- turbidity
- flocculant
- treated water
- raw water
- calculator
- 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.)
- Granted
Links
Abstract
Description
【発明の詳細な説明】
本発明は、水処理における凝集剤の注入制御に関するも
のである0
従来、この種の装置として第1図に示すものがあった。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to injection control of a flocculant in water treatment. Conventionally, there has been an apparatus of this type as shown in FIG. 1.
第1図はフィードバック注入制御装置による従来例を示
し、図において、(1)は原水に凝集剤を注入する急速
攪拌池、(2)は原水濁質と凝集剤を混合させるフロキ
ュレータを含む沈澱池、(3)は上記急速攪拌池(1)
に流入する原水流量を計測する原水流量計、(4)は凝
集剤流量計、(6)は凝集剤流量を操作する凝集剤注入
操作器、(6)は凝集剤流量を制御する制御器、(7)
は原水流量計(8)による原水流量と比率演算器(9)
により求まる注入率より注入量を計算する注入量演算器
、(8)は制御量である処理水濁度を測定する処理水濁
度計、輪は沈澱池出口濁度設定器(ロ)による沈澱池出
口濁度の設定値よシ所望処理水濁度の設定値を計算する
処理水設定濁度演算器である。Figure 1 shows a conventional example using a feedback injection control device. In the figure, (1) is a rapid stirring tank that injects a flocculant into raw water, and (2) is a sedimentation tank that includes a flocculator that mixes the raw water suspended matter and the flocculant. Pond (3) is the above rapid stirring pond (1)
(4) is a flocculant flow meter, (6) is a flocculant injection operator that operates the flocculant flow rate, (6) is a controller that controls the flocculant flow rate, (7)
is the raw water flow rate using the raw water flow meter (8) and the ratio calculator (9)
(8) is a treated water turbidity meter that measures the treated water turbidity, which is a control amount; and the ring is the sedimentation by the settling tank outlet turbidity setting device (b). This is a treated water setting turbidity calculator that calculates the desired treated water turbidity setting value based on the pond outlet turbidity setting value.
第1図構成においては、運転員が沈澱池(2)出口濁度
の設定値を設定器CI劾によって設定すると、その信号
は処理水設定濁度演算器−に送られフィードバック制御
によって制御しようとする処理水濁度の設定値があらか
じめ求められた関数式によって計算される。計算された
処理水濁度の設定値は比率演算器(9)に送られ、ここ
では処理水濁度計(8)による処理水濁度の値と比較さ
れ両者の偏差に応じて凝集剤注入率(比率)が計算され
注入量演算器(7)に送られる。注入量演算器(γ)で
は比率演算器(9)による注入率と原水流量針(3)に
よる原水流量から凝集剤注入量を計算する。そして、こ
の注入量は注入量制御器(6)に送られ、この制御器と
凝集剤流量計(4)のフィードバック信号と操作器(5
)によって適切な凝集剤注入量が急速攪拌池(1)に注
入され、原水と混合されるようになっている。さらに、
この後、原水はフロキュレータで7μツクを形成し、そ
の後方の沈澱池でフロックを沈降させ所望の出口濁度と
なって次のろ過池に入るようになっているO
従来の凝集剤注入制御装置は以上のように構成されてい
るため、処理水濁度演算器に原水流量の信号が入力され
なく、このため、原水流量が変わると、沈澱池(2)出
口濁度と処理水濁度の関数式が変化することに追従でき
なくなシ、常に一定な原水流量の場合しか運用できない
という欠点があつた。In the configuration shown in Fig. 1, when the operator sets the set value of the turbidity at the outlet of the settling tank (2) using the setting device CI, the signal is sent to the treated water setting turbidity calculator and is then controlled by feedback control. The set value of the turbidity of the treated water is calculated using a predetermined functional formula. The calculated treated water turbidity set value is sent to the ratio calculator (9), where it is compared with the treated water turbidity value measured by the treated water turbidity meter (8), and flocculant is injected according to the deviation between the two. A rate (ratio) is calculated and sent to the injection amount calculator (7). The injection amount calculation unit (γ) calculates the amount of flocculant injection from the injection rate determined by the ratio calculation unit (9) and the raw water flow rate determined by the raw water flow rate needle (3). Then, this injection amount is sent to the injection amount controller (6), and a feedback signal from this controller and the flocculant flow meter (4) and an operation device (5) are sent to the injection amount controller (6).
), an appropriate amount of flocculant is injected into the rapid stirring basin (1) and mixed with the raw water. moreover,
After this, the raw water forms a 7μ filter in a flocculator, and the flocs are settled in a settling tank behind it to reach the desired outlet turbidity before entering the next filter tank.O Conventional flocculant injection control Because the device is configured as described above, the raw water flow rate signal is not input to the treated water turbidity calculator. Therefore, when the raw water flow rate changes, the settling tank (2) outlet turbidity and the treated water turbidity change. It has the disadvantage that it cannot follow the changes in the functional formula and can only be used when the raw water flow rate is constant.
本発明は、上記のような従来のものの欠点を除去するた
めになされたもので、原水流量の変化を処理水設定濁度
演算器に送ることによシ、原水流量に応じた処理水濁度
設定値を計算し、これによシ沈澱池出ロ濁度を制御する
ことができるようにした凝集剤注入制御装置を提供する
ことを目的としている。The present invention was made in order to eliminate the drawbacks of the conventional ones as described above, and by sending changes in the raw water flow rate to a treated water setting turbidity calculator, it is possible to adjust the treated water turbidity according to the raw water flow rate. It is an object of the present invention to provide a flocculant injection control device that can calculate a set value and thereby control the turbidity of a sedimentation tank.
以下、本発明の一実施例を第1図と同一部分は同一符号
を附して示す第2図に基いて説明する。Hereinafter, one embodiment of the present invention will be described with reference to FIG. 2, in which the same parts as in FIG. 1 are denoted by the same reference numerals.
第2図において、本発明における処理水設定濁度演算器
(至)には沈澱池出口濁度設定器(ロ)による沈澱池出
口濁度の設定値と共に、原水流量計(8)による原水流
量を入力するようになされている0その他は従来と同様
である。In Fig. 2, the treated water setting turbidity calculator (to) in the present invention includes the setting value of the settling tank outlet turbidity by the settling tank outlet turbidity setting device (b), as well as the raw water flow rate by the raw water flow meter (8). 0, which is inputted, and others are the same as before.
したがって、第2図構成において、運転員が沈澱池出口
濁度の設定値を設定器(ロ)によって設定すると、その
信号は処理水設定濁度演算器叫に送られ、ここではあら
かじめ求められた関数式(原水流量で滞留時間が違うの
で、原水流量によって関数式が違う。)と、原水流量計
(81による原水流量と設定器Qlによる設定値によっ
て処理水設定濁度が計算される。Therefore, in the configuration shown in Figure 2, when the operator sets the set value of the settling tank outlet turbidity using the setting device (B), the signal is sent to the treated water setting turbidity calculator, and here the predetermined value is The set turbidity of the treated water is calculated using the functional formula (residence time differs depending on the raw water flow rate, so the functional formula differs depending on the raw water flow rate), the raw water flow rate from the raw water flow meter (81), and the set value from the setting device Ql.
この後の動作は従来と同様で、計算された処理水濁度の
設定値は比率演算器(9)に送られ、ここでは処理水濁
度計(8)による処理水濁度の値と比較され両者の偏差
に応じて凝集剤注入率(比率)が計算され注入量演算、
器(γ)に送られる。注入量演算器(9)による注入率
と原水流量計(8)による原水流量から凝集剤注入量を
計算する◇そして、この注入量は注入量制御器(6)に
送られ、と、の制御器と凝集剤流量計(4)のフィード
バック信号と操作器(6)によって適切な凝集剤注入量
が急速攪拌池(1)に注入され、原水と混合されるよう
になっている。さらに、この後、原水はフロキュレータ
で70ツクを形成し、その後方の沈澱池で70ツクを沈
降させ所望の出口濁度となって次のろ過池に入るように
なっている0
なお、上記実施例ではフィードバック制御について述べ
たが、フィードバック制御とフィードバック制御を組み
合わせた場合も同様の効果を奏するのは勿論である。The subsequent operation is the same as before, and the calculated treated water turbidity set value is sent to the ratio calculator (9), where it is compared with the treated water turbidity value measured by the treated water turbidity meter (8). The flocculant injection rate (ratio) is calculated according to the deviation between the two, and the injection amount is calculated.
is sent to the container (γ). The flocculant injection amount is calculated from the injection rate by the injection amount calculator (9) and the raw water flow rate by the raw water flow meter (8) ◇Then, this injection amount is sent to the injection amount controller (6). An appropriate amount of coagulant is injected into the rapid stirring basin (1) by means of feedback signals from the flocculant flow meter (4) and the operating device (6), and is mixed with the raw water. Furthermore, after this, the raw water forms 70 filters in the flocculator, and settles 70 filters in the settling tank behind it to reach the desired outlet turbidity before entering the next filter tank. Although feedback control has been described in the embodiment, it goes without saying that the same effect can be achieved by combining feedback control and feedback control.
以上のように本発明によれば、原水流量の信号を処理水
設定濁度演算器に入力したので、原水流量が変っても容
易に沈澱池出口濁度を設定値に制御でき安定した濁度の
水が得られる効果がある。As described above, according to the present invention, since the raw water flow rate signal is input to the treated water setting turbidity calculator, the sedimentation tank outlet turbidity can be easily controlled to the set value even if the raw water flow rate changes, and stable turbidity can be maintained. of water.
第1図は従来の凝集剤注入制御装置を示す構成図、第2
図は本発明の一実施例による凝集剤注入制御装置を示す
構成図である。
(1)・・急速攪拌池 (2)・・沈澱池(3)・・
原水流量計 (4)・・凝集剤流量計(5)・・凝集
剤注入操作器
(θ)拳・注入量制御器
())・・注入量演算器
(8)・・処理水濁度計
(9)・−比率演算器
酸、(2)−・処理水設定濁度演算器
o3J+1・沈澱池出口濁度設定器Figure 1 is a configuration diagram showing a conventional flocculant injection control device, Figure 2
The figure is a configuration diagram showing a flocculant injection control device according to an embodiment of the present invention. (1)... Rapid stirring tank (2)... Sedimentation tank (3)...
Raw water flow meter (4)...Flocculant flow meter (5)...Flocculant injection operator (θ) fist/injection rate controller ())...Injection rate calculator (8)...Treatment water turbidity meter (9) - Ratio calculator acid, (2) - Treated water setting turbidity calculator o3J+1, Sedimentation tank outlet turbidity setter
Claims (1)
理水濁度を測定する処理水濁度計と、沈澱池出口濁度を
設定する設定器と、上記設定器による設定値と原水流量
とによシ処理水の濁度設定値を計算する演算器と、上記
処理水濁度計によ為処理水濁度と前記演算器による設定
値より凝集剤注入比率を計算する比率演算器と、上記比
率演算器による比率と原水流量により凝集剤注入量を計
算する注入量演算器と、凝集剤注入量を制御する注入量
制御器と、凝集剤注入操作器、及び凝集剤流量計とを備
えた水処理における凝集剤注入制御装置。A raw water flow meter that measures the flow rate of raw water to remove turbidity, a treated water turbidity meter that measures the turbidity of treated water, a setting device that sets the turbidity at the outlet of the sedimentation tank, and the settings by the above setting device and the raw water. a calculator that calculates the flow rate and the turbidity set value of the treated water; and a ratio calculator that calculates the flocculant injection ratio from the turbidity of the treated water collected by the treated water turbidity meter and the set value by the calculator. , an injection amount calculator that calculates the flocculant injection amount based on the ratio by the ratio calculator and the raw water flow rate, an injection amount controller that controls the flocculant injection amount, a flocculant injection operator, and a flocculant flow meter. A flocculant injection control device for water treatment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13989581A JPS5840115A (en) | 1981-09-03 | 1981-09-03 | Flocculant pouring control apparatus in water treatment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13989581A JPS5840115A (en) | 1981-09-03 | 1981-09-03 | Flocculant pouring control apparatus in water treatment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5840115A true JPS5840115A (en) | 1983-03-09 |
JPS631885B2 JPS631885B2 (en) | 1988-01-14 |
Family
ID=15256106
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13989581A Granted JPS5840115A (en) | 1981-09-03 | 1981-09-03 | Flocculant pouring control apparatus in water treatment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5840115A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6054832U (en) * | 1983-09-22 | 1985-04-17 | 藤井電工株式会社 | Hook with built-in alarm device |
JPH05168819A (en) * | 1991-12-26 | 1993-07-02 | Hitachi Plant Eng & Constr Co Ltd | Method for purifying water and device therefor |
-
1981
- 1981-09-03 JP JP13989581A patent/JPS5840115A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6054832U (en) * | 1983-09-22 | 1985-04-17 | 藤井電工株式会社 | Hook with built-in alarm device |
JPH05168819A (en) * | 1991-12-26 | 1993-07-02 | Hitachi Plant Eng & Constr Co Ltd | Method for purifying water and device therefor |
Also Published As
Publication number | Publication date |
---|---|
JPS631885B2 (en) | 1988-01-14 |
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