JPH05169082A - Control unit for injection quantity of chemical - Google Patents
Control unit for injection quantity of chemicalInfo
- Publication number
- JPH05169082A JPH05169082A JP3343810A JP34381091A JPH05169082A JP H05169082 A JPH05169082 A JP H05169082A JP 3343810 A JP3343810 A JP 3343810A JP 34381091 A JP34381091 A JP 34381091A JP H05169082 A JPH05169082 A JP H05169082A
- Authority
- JP
- Japan
- Prior art keywords
- injection
- scum
- circuit
- aeration tank
- chemical
- 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
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Activated Sludge Processes (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、下水道水処理プラント
に使用する薬品注入量制御装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a chemical injection amount control device used in a sewer water treatment plant.
【0002】[0002]
【従来の技術】従来の技術で、連続制御的な方法でな
く、タイマーなどを使ったシーケンシャルな運転方法が
行われ、運転判断も操作員によるもの、またはスカムの
発生量の判定によるもので、薬品注入は定量の注入方法
であった。2. Description of the Related Art In the prior art, a sequential driving method using a timer or the like is performed instead of a continuous control method, and the driving judgment is made by an operator or by judging the amount of scum generated, Chemical injection was a constant injection method.
【0003】[0003]
【発明が解決しようとする課題】従来は、定量的なバッ
チ注入法の為に、薬品使用量の無駄が発生したり、スカ
ムが発生してから薬品注入する運転方法がとられる為
に、スカム発生伝策の予防が遅れ、処理不充分なスカム
が混合した水が流出するという不具合があった。Conventionally, since a quantitative batch injection method has resulted in waste of the amount of chemicals used and an operation method in which chemicals are injected after scum is generated, scum is used. There was a problem that the prevention of the transmission policy was delayed and the water mixed with the insufficiently treated scum leaked out.
【0004】[0004]
【課題を解決するための手段】本発明は、エアレーショ
ンタンクの水温を検出する水温計と、エアレーションタ
ンクの処理水のPH値を検出するPH計と、最終沈殿池
で採集されたスカムの重量を計測するスカム重量計と、
エアレーションタンクに流入する処理水の流量を計測す
る流入量流量計と、水温及びPH値からエアレーション
タンクに注入する薬品の注入率を算出する注入率設定演
算回路と、この注入率設定演算回路からの出力信号及び
流入量流量計の出力信号からエアレーションタンクに注
入する薬品の注入量を算出する注入量設定回路と、この
注入量設定回路から出力された注入量設定値をスカム重
量計の出力値で補正する注入量補正回路と、この注入量
補正回路の出力に薬品注入量を加味して制御するPID
制御回路と、このPID制御回路の出力値で薬品を注入
する注入ポンプの運転速度を制御する速度制御装置と、
を具備してなる薬品注入量制御装置である。According to the present invention, a water thermometer for detecting the water temperature of an aeration tank, a PH meter for detecting a PH value of treated water in the aeration tank, and a weight of scum collected in a final settling tank are measured. With a scum scale to measure
An inflow rate flow meter that measures the flow rate of treated water flowing into the aeration tank, an injection rate setting calculation circuit that calculates the injection rate of the chemicals to be injected into the aeration tank from the water temperature and PH value, and an injection rate setting calculation circuit from this injection rate setting calculation circuit. The injection amount setting circuit that calculates the injection amount of the chemicals to be injected into the aeration tank from the output signal and the output signal of the flowmeter and the injection amount setting value output from this injection amount setting circuit is the output value of the scum scale. An injection amount correction circuit for correction and a PID for controlling the output of the injection amount correction circuit by adding the amount of chemical injection
A control circuit and a speed control device for controlling an operating speed of an infusion pump for injecting a chemical with an output value of the PID control circuit,
It is a chemical injection amount control device comprising.
【0005】[0005]
【作用】本発明による薬品注入量制御装置においては、
エアレーションタンクの水温を検出し、エアレーション
タンクの処理水のPH値を検出し、最終沈殿池で採集さ
れたスカムの重量を計測し、エアレーションタンクに流
入する処理水の流量を計測し、水温及びPH値からエア
レーションタンクに注入する薬品の注入率を算出し、注
入率設定演算回路からの出力信号及び流入量流量計の出
力信号からエアレーションタンクに注入する薬品の注入
量を算出し、注入量設定回路から出力された注入量設定
値をスカム重量計の出力値で補正し、注入量補正回路の
出力に薬品注入量を加味して制御し、このPID制御回
路の出力値で薬品を注入する注入ポンプの運転速度を制
御する。In the chemical injection amount control device according to the present invention,
The water temperature of the aeration tank is detected, the PH value of the treated water in the aeration tank is detected, the weight of the scum collected in the final settling tank is measured, and the flow rate of the treated water flowing into the aeration tank is measured to determine the water temperature and PH. Calculate the injection rate of the chemicals to be injected into the aeration tank from the values, calculate the injection rate of the chemicals to be injected into the aeration tank from the output signal from the injection rate setting calculation circuit and the output signal of the inflow rate flow meter, and set the injection rate setting circuit. The injection pump that corrects the set value of the injection amount output from the scum scale and controls the output of the injection amount correction circuit by adding the injection amount of the drug, and injects the drug with the output value of this PID control circuit. Control the driving speed of.
【0006】[0006]
【実施例】次に、本発明の一実施例を説明する。図1
は、エアレーションタンク20の水温を検出する水温計12
と、エアレーションタンク20の処理水のPH値を検出す
るPH計11と、最終沈殿池21で採集されたスカムの重量
を計測するスカム重量計15と、エアレーションタンク20
に流入する処理水の流量を計測する流入量流量計10と、
水温及びPH値からエアレーションタンク20に注入する
薬品の注入率を算出する注入率設定演算回路3と、注入
率設定演算回路3からの出力信号及び流入量流量計10の
出力信号からエアレーションタンク20に注入する薬品の
注入量を算出する注入量設定回路4と、注入量設定回路
4から出力された注入量設定値をスカム重量計15の出力
値で補正する注入量補正回路5と、注入量補正回路5の
出力に薬品注入量を加味して制御するPID制御回路22
と、PID制御回路22の出力値で薬品を注入する注入ポ
ンプ14の運転速度を制御する速度制御装置23と、を具備
してなる薬品注入量制御装置であり、スカム浮上を抑制
する目的で、薬品注入(凝集剤として硫酸バンドなど)
する制御回路でエアレーションタンクの温度PH及びス
カム発生重量より判定し注入制御開始する回路、スカム
発生重量より制御停止する回路、エアレーションタンク
の温度、PHより求めた特性関数より注入率係数を算出
し流入水量との乗算演算し求めた薬品注入量にスカム発
生重量に比例した補正値を加算演算し最適薬品注入量を
目標値としてPID制御をする。EXAMPLE An example of the present invention will be described below. Figure 1
Is a water temperature gauge 12 that detects the water temperature of the aeration tank 20.
A pH meter 11 for detecting the pH value of the treated water in the aeration tank 20, a scum weight meter 15 for measuring the weight of scum collected in the final settling tank 21, and an aeration tank 20.
An inflow flowmeter 10 for measuring the flow rate of the treated water flowing into the
The injection rate setting calculation circuit 3 for calculating the injection rate of the chemical to be injected into the aeration tank 20 from the water temperature and the PH value, and the output signal from the injection rate setting calculation circuit 3 and the output signal of the inflow rate flowmeter 10 to the aeration tank 20. An injection amount setting circuit 4 for calculating the injection amount of the medicine to be injected, an injection amount correction circuit 5 for correcting the injection amount setting value output from the injection amount setting circuit 4 with the output value of the scum scale 15, and an injection amount correction PID control circuit 22 that controls the output of circuit 5 by adding the chemical injection amount
And a speed control device 23 for controlling the operating speed of the infusion pump 14 for injecting a drug with the output value of the PID control circuit 22, and for the purpose of suppressing scum levitation. Chemical injection (sulfuric acid band etc. as coagulant)
A control circuit determines the injection rate from the aeration tank temperature PH and the weight of scum generated, and starts injection control, a circuit that stops the control based on the weight of scum generated, the aeration tank temperature, and calculates the injection rate coefficient from the characteristic function obtained from the inflow. A correction value proportional to the amount of scum generated is added to the amount of chemical injection calculated by multiplication with the amount of water, and PID control is performed with the optimum amount of chemical injection as the target value.
【0007】即ち、薬品使用量の無駄を防ぐ為に、バッ
チ制御法から連続制御法とし、最適な連続制御法とする
為に、流入水量の計測及びスカムの発生し易い環境状態
を把握する目的でエアレーションタンク内のPH・温度
の計測を行ない、薬品注入率は通常40g/ m3 前後
で、従来の方法では定量的に一定時間薬品注入するが、
本制御では、流入下水の温度、PHによる要因で薬品注
入率を決め最適な注入量を求める方法をとり、流入下水
の水温及びPHの要因で薬品注入率を決める事は以下の
理由によるところである。That is, in order to prevent the waste of the amount of chemicals used, the batch control method is changed to the continuous control method, and the purpose is to measure the inflow water amount and grasp the environmental condition where scum is likely to occur in order to achieve the optimum continuous control method. The PH and temperature in the aeration tank are measured with a chemical injection rate of around 40 g / m 3, which is a conventional method for quantitative chemical injection for a certain period of time.
In this control, the chemical injection rate is determined by factors such as the temperature of the inflowing sewage and PH to determine the optimum injection amount, and the chemical injection rate is determined by the factors of the inflowing sewage water temperature and PH for the following reasons. ..
【0008】即ち、スカム発生の原因としては、放射菌
がエアレーションタンク内で異常に増殖する為といわれ
ており、その主たる微生物がノカルディアアマラル(No
cardia amaral )と推定されており、このノカルディア
(Nocardia)を増殖させる環境要因に温度とPHが関係
しており、図2及び図3にこれらの増殖度を示す相関図
を表わす。図で示す通り、24〜30℃、7.0 〜8.5 PHの
付近がノカルディア(Nocardia)の増殖量が大きい。従
って、この付近でのスカム発生量の増大が予想され薬品
率も図1、図2の相関に従った率とする。[0008] That is, it is said that the cause of the scum is that the radiant bacteria abnormally proliferate in the aeration tank, and the main microorganism is Nocardia amaral (No.
cardia amaral), and temperature and PH are related to the environmental factors for growing this Nocardia, and FIGS. 2 and 3 show correlation diagrams showing the degree of growth. As shown in the figure, the growth amount of Nocardia is large near 24 to 30 ° C and 7.0 to 8.5 PH. Therefore, it is expected that the amount of scum generated in this vicinity will increase, and the chemical rate will also follow the correlation shown in FIGS.
【0009】そして、図1の1はPH計の特性演算回路
で、図2に示すような特性関係を示す。PH値6.5 〜8.
0 PHに於いて、関数出力(PH)は0.5 〜1.2 の変数
値を示す。Reference numeral 1 in FIG. 1 denotes a characteristic operation circuit of the PH meter, which shows a characteristic relationship as shown in FIG. PH value 6.5 to 8.
At 0 PH, the function output (PH) shows a variable value of 0.5 to 1.2.
【0010】図1の2は温度の特性演算回路で、図3に
示すような特性関数を示す。温度25℃〜30℃に於いて、
関数出力f(τ)は0.5 〜1.2 の変数値を示す。Reference numeral 2 in FIG. 1 is a temperature characteristic calculation circuit, which shows a characteristic function as shown in FIG. At a temperature of 25 ℃ to 30 ℃,
The function output f (τ) shows a variable value of 0.5 to 1.2.
【0011】また、図1の3は注入率設定演算回路で、
エアレーションタンク内の水質に応じた薬品の注入率を
決定する回路である。Reference numeral 3 in FIG. 1 is an injection rate setting arithmetic circuit.
It is a circuit that determines the injection rate of chemicals according to the water quality in the aeration tank.
【0012】αo =α(αi f(PH)・fα2 ・f
(τ))の式で表わすもので、注入率ディメンションと
してはg/m3 である。Α o = α (α i f (PH) · fα 2 · f
(Τ)), and the injection rate dimension is g / m 3 .
【0013】尚、ここでα1 は0.3 〜0.6 ,α2 は0.3
〜0.6 ,αは通常40g/m3 であり注入率α0 は12g/
m3 〜57.6g/m3 の値をとる。Here, α 1 is 0.3 to 0.6 and α 2 is 0.3
~ 0.6, α is usually 40 g / m 3 and injection rate α 0 is 12 g / m 3.
It takes a value of m 3 to 57.6 g / m 3 .
【0014】注入量設定回路4では、上記の注入率と流
入下水量を乗算し、目標とする薬液量を求める。In the injection amount setting circuit 4, the above injection rate is multiplied by the inflowing sewage amount to obtain a target amount of chemical liquid.
【0015】次に、注入量補正回路5では、注入量設定
回路4で設定した目標の注入量設定値に対して、スカム
重量計15による信号でスカム発生量に比例した補正を行
なうものである。演算式では、 α0 F+K・Wとする。Next, in the injection amount correction circuit 5, the target injection amount setting value set by the injection amount setting circuit 4 is corrected by a signal from the scum weight scale 15 in proportion to the scum generation amount. .. In the calculation formula, α 0 F + K · W.
【0016】尚、Kは0.001 〜0.01の定数,Wはスカム
発生重量(g)である。Incidentally, K is a constant of 0.001 to 0.01, and W is a scum generation weight (g).
【0017】そして、注入量補正回路5の出力信号を目
標量として、薬品の注入PID制御を行なうものであ
る。Then, the injection PID control of the medicine is performed by using the output signal of the injection amount correction circuit 5 as a target amount.
【0018】本制御は、スカムの発生し易い状態のと
き、予め運転させるような回路を信号判定回路6,7及
び運転判定回路8で運転指令をかけるようにしている。In the present control, when the scum is likely to occur, the signal determination circuits 6 and 7 and the operation determination circuit 8 issue an operation command for a circuit which is operated in advance.
【0019】信号判定回路6ではエアレーションタンク
内のPH、信号判定回路7では温度の判定回路で、スカ
ムの発生し易い環境条件を判定し、更にスカムの発生量
が規定量以上であるかを運転判定回路8で判定し、運転
指令をかける。The signal judging circuit 6 uses the PH in the aeration tank, and the signal judging circuit 7 uses the temperature judging circuit to judge the environmental conditions in which scum is likely to occur. Judgment is made by the judgment circuit 8 and an operation command is issued.
【0020】スカムが規定重量以下になった場合にはタ
イミングも考慮して停止判定回路9で停止させるもので
ある。When the scum becomes less than the specified weight, the stop determination circuit 9 is used in consideration of the timing.
【0021】本制御で使用する薬品は、凝集剤として良
く使用される硫酸バンドを通常使っており、硫酸バンド
自体、酸性薬品の為、図2のPH値特性に示されるよ
う、酸性にする事でスカムの発生が抑えられる。温度が
25℃近辺でスカムの発生が高くなる要因があるので、こ
の近辺では薬品量を多く注入する事でスカム発生量を抑
える効果が高い。更にスカム重量計をとりつける事でス
カム発生量に相関した薬品注入をする。これらの要素
で、薬品の効果的な使用が計られる。As the chemical used in this control, a sulfuric acid band which is often used as a coagulant is usually used. Since the sulfuric acid band itself is an acidic chemical, it should be acidified as shown in the PH value characteristic of FIG. Therefore, the generation of scum is suppressed. temperature
Since there is a factor that scum generation becomes high near 25 ° C, it is highly effective to suppress the scum generation by injecting a large amount of chemicals around this. Furthermore, by mounting a scum scale, chemical injection that correlates with the amount of scum generated can be injected. These factors measure the effective use of medicines.
【0022】[0022]
【発明の効果】スカム発生要因を制御演算回路にとり込
む事で薬品注入量の最適な最定が可能である。EFFECT OF THE INVENTION By incorporating the scum generation factor into the control arithmetic circuit, it is possible to optimally determine the chemical injection amount.
【0023】それにより省資源化の効果が大である。ま
た、注入開始をスカム発生量、エアレーションタンク内
の環境状態で判断している為、従来人が判断するよりも
より規格化された判定ができ、プラント運転の不安定化
を防ぐ事ができる。As a result, the effect of resource saving is great. In addition, since the start of injection is determined based on the amount of scum generated and the environmental condition in the aeration tank, it is possible to make a more standardized determination than the determination made by a conventional person, and prevent instability in plant operation.
【図1】本発明の一実施例を示す薬品注入量制御装置の
構成図である。FIG. 1 is a configuration diagram of a chemical injection amount control device showing an embodiment of the present invention.
【図2】PH特性の説明図である。FIG. 2 is an explanatory diagram of PH characteristics.
【図3】温度特性の説明図である。FIG. 3 is an explanatory diagram of temperature characteristics.
3…注入率設定演算回路 4…注入量設定回路 5…注入量補正回路 11…PH計 12…水温計 15…スカム重量計 14…注入ポンプ 20…エアレーションタンク 22…PID制御回路 23…速度制御装置 3 ... injection rate setting arithmetic circuit 4 ... injection amount setting circuit 5 ... injection amount correction circuit 11 ... PH meter 12 ... water thermometer 15 ... scum weight scale 14 ... injection pump 20 ... aeration tank 22 ... PID control circuit 23 ... speed control device
Claims (1)
水温計と、前記エアレーションタンクの処理水のPH値
を検出するPH計と、最終沈殿池で採集されたスカムの
重量を計測するスカム重量計と、前記エアレーションタ
ンクに流入する処理水の流量を計測する流入量流量計
と、前記水温及び前記PH値から前記エアレーションタ
ンクに注入する薬品の注入率を算出する注入率設定演算
回路と、この注入率設定演算回路からの出力信号及び前
記流入量流量計の出力信号から前記エアレーションタン
クに注入する薬品の注入量を算出する注入量設定回路
と、この注入量設定回路から出力された注入量設定値を
前記スカム重量計の出力値で補正する注入量補正回路
と、この注入量補正回路の出力に薬品注入量を加味して
制御するPID制御回路と、このPID制御回路の出力
値で前記薬品を注入する注入ポンプの運転速度を制御す
る速度制御装置と、を具備してなる薬品注入量制御装
置。1. A water thermometer for detecting a water temperature of an aeration tank, a PH meter for detecting a PH value of treated water in the aeration tank, and a scum scale for measuring the weight of scum collected in a final settling tank. An inflow rate flow meter for measuring the flow rate of treated water flowing into the aeration tank, an injection rate setting arithmetic circuit for calculating an injection rate of a chemical to be injected into the aeration tank from the water temperature and the PH value, and an injection rate setting The injection amount setting circuit for calculating the injection amount of the chemical to be injected into the aeration tank from the output signal from the arithmetic circuit and the output signal of the inflow amount flowmeter, and the injection amount setting value output from the injection amount setting circuit An injection amount correction circuit that corrects the output value of the scum scale, and a PID control circuit that controls the output of the injection amount correction circuit by adding the amount of chemical injection. And a speed control device for controlling the operating speed of an infusion pump for injecting the drug with the output value of the PID control circuit.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3343810A JP3043880B2 (en) | 1991-12-26 | 1991-12-26 | Chemical injection amount control device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3343810A JP3043880B2 (en) | 1991-12-26 | 1991-12-26 | Chemical injection amount control device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05169082A true JPH05169082A (en) | 1993-07-09 |
JP3043880B2 JP3043880B2 (en) | 2000-05-22 |
Family
ID=18364413
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3343810A Expired - Fee Related JP3043880B2 (en) | 1991-12-26 | 1991-12-26 | Chemical injection amount control device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3043880B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07148482A (en) * | 1993-11-29 | 1995-06-13 | Hidekazu Murotani | Method and apparatus for controlling hydrogen sulfide in waste water chemical injection |
JP2002307094A (en) * | 2001-04-13 | 2002-10-22 | Toshiba Corp | Sewage treatment system |
JP5190598B1 (en) * | 2012-08-03 | 2013-04-24 | 強化土株式会社 | Ground injection device and ground injection method |
-
1991
- 1991-12-26 JP JP3343810A patent/JP3043880B2/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07148482A (en) * | 1993-11-29 | 1995-06-13 | Hidekazu Murotani | Method and apparatus for controlling hydrogen sulfide in waste water chemical injection |
JP2002307094A (en) * | 2001-04-13 | 2002-10-22 | Toshiba Corp | Sewage treatment system |
JP5190598B1 (en) * | 2012-08-03 | 2013-04-24 | 強化土株式会社 | Ground injection device and ground injection method |
Also Published As
Publication number | Publication date |
---|---|
JP3043880B2 (en) | 2000-05-22 |
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