JP2003047805A - Water treatment apparatus and apparatus for adjusting quantity of flocculant to be added - Google Patents

Water treatment apparatus and apparatus for adjusting quantity of flocculant to be added

Info

Publication number
JP2003047805A
JP2003047805A JP2001238176A JP2001238176A JP2003047805A JP 2003047805 A JP2003047805 A JP 2003047805A JP 2001238176 A JP2001238176 A JP 2001238176A JP 2001238176 A JP2001238176 A JP 2001238176A JP 2003047805 A JP2003047805 A JP 2003047805A
Authority
JP
Japan
Prior art keywords
coagulant
addition amount
value
water
adjusting
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.)
Withdrawn
Application number
JP2001238176A
Other languages
Japanese (ja)
Inventor
Naoya Kawarabayashi
直也 河原林
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP2001238176A priority Critical patent/JP2003047805A/en
Publication of JP2003047805A publication Critical patent/JP2003047805A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5209Regulation methods for flocculation or precipitation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/78Treatment of water, waste water, or sewage by oxidation with ozone
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/11Turbidity

Abstract

PROBLEM TO BE SOLVED: To provide a water treatment apparatus in which the degradation of the quality of treated water or the excessive addition of a flocculant is prevented. SOLUTION: The water treatment apparatus is provided with a flocculation reaction tank 1, a flocculant supply part 2, a settling tank 3 and apparatuses 4 and 5 for adjusting the quantity of a flocculant to be added. The apparatus 5 for adjusting the quantity of the flocculant to be added is provided with a detecting means 11 for detecting the turbidity of the treated water and an adjusting means 13 for adjusting the quantity of the flocculant to be added based on the detected value of the detecting means 11. When the detected value by the detecting means 11 is in a predetermined range, the flocculant of the quantity corresponding to the detected value is added and when the detected value becomes lower than the lower limit S1 in the set range, the flocculant is added upto a prescribed value V1 .

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、用水(河川水、湖
水、井水等)、産業排水などに含まれる懸濁物質等を凝
集剤を用いて凝集させ、分離する水処理装置およびこれ
に用いられる凝集剤添加量調節装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water treatment device for aggregating suspended substances contained in irrigation water (river water, lake water, well water, etc.), industrial wastewater, etc. using a coagulant and separating the same. The present invention relates to a coagulant addition amount adjusting device used.

【0002】[0002]

【従来の技術】従来より、用水、排水などに含まれる懸
濁物質等を凝集剤を用いて凝集沈殿させて分離するにあ
たり、凝集剤を過不足なく添加するため、処理水の濁度
の検出値に基づいて、PI制御、PID制御、ファジー
制御などにより凝集剤の添加量を制御することが提案さ
れている。例えば、特開平2−261505号公報およ
び特開平2−258004号公報には、処理水濁度等に
基づいて、ファジー制御により凝集剤添加量を制御する
方法が開示されている。
2. Description of the Related Art Conventionally, when a suspended substance contained in water, waste water, etc. is coagulated and precipitated using a coagulant to separate it, the coagulant is added just enough to detect the turbidity of treated water. It has been proposed to control the addition amount of the coagulant by PI control, PID control, fuzzy control, etc. based on the value. For example, JP-A-2-261505 and JP-A-2-258004 disclose a method of controlling the coagulant addition amount by fuzzy control based on the turbidity of treated water and the like.

【0003】図3は、従来の水処理装置の一例を示すも
のである。図3において、符号1は、被処理水が導入さ
れる凝集反応槽を示し、符号2は、凝集剤を供給する凝
集剤供給部を示し、符号3は、凝集物を沈降分離する沈
澱槽を示し、符号4は、凝集剤供給部2からの凝集剤を
添加量調節して凝集反応槽1に添加する凝集剤添加量調
節装置を示す。凝集剤供給部2は、凝集剤溶液を貯留す
る凝集剤貯留槽6を備えている。凝集剤添加量調節装置
4は、被処理水の流量を検出する流量計7と、被処理水
の濁度を検出する濁度計8と、これらからの検出信号に
基づいて駆動信号を出力する制御部9と、制御部9から
の駆動信号に基づいて、凝集剤貯留槽6からの凝集剤溶
液の流量を調節する送液ポンプ10とを備えている。
FIG. 3 shows an example of a conventional water treatment device. In FIG. 3, reference numeral 1 indicates a flocculation reaction tank into which water to be treated is introduced, reference numeral 2 indicates a flocculant supply unit for supplying a flocculant, and reference numeral 3 indicates a precipitation tank for settling and separating flocculates. Reference numeral 4 denotes a coagulant addition amount adjusting device for adjusting the addition amount of the coagulant from the coagulant supply unit 2 and adding it to the coagulation reaction tank 1. The coagulant supply unit 2 includes a coagulant storage tank 6 that stores the coagulant solution. The coagulant addition amount adjusting device 4 outputs a drive signal based on a flow meter 7 for detecting the flow rate of the water to be treated, a turbidity meter 8 for detecting the turbidity of the water to be treated, and detection signals from these. The controller 9 and the liquid feed pump 10 that adjusts the flow rate of the coagulant solution from the coagulant storage tank 6 based on the drive signal from the controller 9 are provided.

【0004】この水処理装置では、供給経路L1を通し
て被処理水を凝集反応槽1に導入するとともに、凝集剤
貯留槽6からの凝集剤溶液を凝集反応槽1に添加して、
被処理水中の懸濁物質等を凝集させ、凝集物を沈澱槽3
で沈降分離し、処理水を得る。
In this water treatment apparatus, the water to be treated is introduced into the flocculation reaction tank 1 through the supply path L1, and the flocculant solution from the flocculant storage tank 6 is added to the flocculation reaction tank 1.
Suspended substances, etc. in the water to be treated are aggregated, and the aggregates are settling tank 3
To separate treated water to obtain treated water.

【0005】凝集剤の添加量は、流量計7および濁度計
8によって検出された被処理水の流量および濁度に基づ
いて定められる。すなわち、流量計7および濁度計8か
らの検出信号に基づいて制御部9から駆動信号が出力さ
れ、この駆動信号に応じて送液ポンプ10が駆動し、供
給経路L4からの凝集剤溶液の流量が定められる。これ
によって、被処理水の流量および濁度に応じた量の凝集
剤が凝集反応槽1に添加される。
The addition amount of the coagulant is determined based on the flow rate and turbidity of the water to be treated detected by the flow meter 7 and the turbidity meter 8. That is, a drive signal is output from the control unit 9 based on the detection signals from the flow meter 7 and the turbidimeter 8, the liquid feed pump 10 is driven according to this drive signal, and the coagulant solution from the supply path L4 is discharged. The flow rate is defined. As a result, an amount of the aggregating agent depending on the flow rate and turbidity of the water to be treated is added to the aggregating reaction tank 1.

【0006】図4は、従来の水処理装置の他の例を示す
もので、ここに示す水処理装置は、凝集剤貯留槽6から
の凝集剤溶液を一定の流量で凝集反応槽1に供給する凝
集剤供給部14を備えている。凝集剤供給部14は、供
給経路L6と送液ポンプ15とを備えている。この水処
理装置では、調節装置4によって、被処理水の流量、濁
度の検出値に応じた量の凝集剤が凝集反応槽1に添加さ
れ、かつ凝集剤供給部14によって、一定流量で凝集剤
が添加される。
FIG. 4 shows another example of the conventional water treatment apparatus. The water treatment apparatus shown here supplies the flocculant solution from the flocculant storage tank 6 to the flocculation reaction tank 1 at a constant flow rate. The coagulant supply unit 14 is provided. The coagulant supply unit 14 includes a supply path L6 and a liquid feed pump 15. In this water treatment device, the coagulant in an amount corresponding to the flow rate of the water to be treated and the detected value of turbidity is added to the coagulation reaction tank 1 by the controller 4, and the coagulant supply unit 14 coagulates the coagulant at a constant flow rate. Agent is added.

【0007】[0007]

【発明が解決しようとする課題】しかしながら、上記従
来技術では、濁度計への懸濁物質付着や気泡混入、濁度
計の故障などによって、検出値が不正確になることがあ
る。検出値が実際の処理水濁度よりも低くなると、凝集
剤添加量が不足し、処理水質が悪化することになる。ま
た検出値が実際の処理水濁度よりも高くなると、凝集剤
添加量が過剰となり、凝集剤に要するコストが高騰する
ことになる。
However, in the above-mentioned conventional technique, the detected value may be inaccurate due to adhesion of suspended solids to the turbidimeter, inclusion of bubbles, failure of the turbidimeter, and the like. If the detected value becomes lower than the actual turbidity of the treated water, the amount of coagulant added will be insufficient and the quality of the treated water will deteriorate. Further, when the detected value becomes higher than the actual turbidity of the treated water, the amount of the coagulant added becomes excessive and the cost required for the coagulant increases.

【0008】濁度計の作動不良を防ぐためには、濁度計
に洗浄機能を付与したり、処理水を脱気処理することに
よって、懸濁物質付着や気泡混入を防止するのが有効で
ある。しかしながら、これらの対策をとった場合でも、
濁度計の作動不良を完全に防ぐのは難しいのが現状であ
り、上記処理水質悪化や凝集剤の過剰添加が起きること
があった。本発明は、上記事情に鑑みてなされたもの
で、処理水質悪化や凝集剤の過剰添加を防ぐことができ
る水処理装置を提供することを目的とする。
In order to prevent the malfunction of the turbidimeter, it is effective to add a cleaning function to the turbidimeter or deaerate the treated water to prevent the adherence of suspended substances and the inclusion of air bubbles. . However, even if these measures are taken,
At present, it is difficult to completely prevent the malfunction of the turbidimeter, and the deterioration of the quality of the treated water and the excessive addition of the coagulant may occur. The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a water treatment device capable of preventing deterioration of treated water quality and excessive addition of a coagulant.

【0009】[0009]

【課題を解決するための手段】本発明の水処理装置は、
被処理水が導入される凝集反応槽と、凝集剤を供給する
凝集剤供給部と、凝集物を分離する固液分離部と、凝集
剤供給部からの凝集剤を添加量調節して凝集反応槽に添
加する複数の凝集剤添加量調節装置とを備え、凝集剤添
加量調節装置のうち少なくとも1つが、処理水の濁度を
検出する検出手段と、検出手段の検出値に基づいて凝集
剤添加量を調節する調節手段とを備え、検出手段の検出
値が予め定めた設定範囲内にあるときに、検出値に応じ
た量の凝集剤が添加され、かつ検出値が設定範囲の下限
値S1未満となったときに、凝集剤添加量が所定の値V1
となるように設定できるようにされていることを特徴と
する。本発明の水処理装置は、被処理水が導入される凝
集反応槽と、凝集剤を供給する凝集剤供給部と、凝集物
を分離する固液分離部と、凝集剤供給部からの凝集剤を
添加量調節して凝集反応槽に添加する複数の凝集剤添加
量調節装置とを備え、凝集剤添加量調節装置のうち少な
くとも1つは、処理水の濁度を検出する検出手段と、検
出手段の検出値に基づいて凝集剤添加量を調節する調節
手段とを備え、検出手段の検出値が予め定めた設定範囲
内にあるときに、検出値に応じた量の凝集剤が添加さ
れ、かつ検出値が所定時間T以上、設定範囲の上限値S
2を越えたときに、凝集剤添加量が所定値V2となるよう
に設定できるようにされた構成とすることができる。前
記凝集剤添加量調節装置は、検出手段の検出値が設定範
囲下限値S1未満となったときに、凝集剤添加量が所定
の値V1となるように設定できるようにすることができ
る。
The water treatment apparatus of the present invention comprises:
A coagulation reaction tank into which water to be treated is introduced, a coagulant supply unit that supplies a coagulant, a solid-liquid separation unit that separates coagulates, and a coagulation reaction by adjusting the amount of coagulant added from the coagulant supply unit. A plurality of coagulant addition amount adjusting devices to be added to the tank, wherein at least one of the coagulant addition amount adjusting devices detects the turbidity of the treated water, and the coagulant based on the detection value of the detecting device. With the adjusting means for adjusting the addition amount, when the detection value of the detecting means is within a predetermined setting range, an amount of the aggregating agent according to the detection value is added, and the detection value is the lower limit value of the setting range. When it becomes less than S 1 , the coagulant addition amount is a predetermined value V 1
It is characterized in that it can be set so that The water treatment apparatus of the present invention includes a flocculation reaction tank into which water to be treated is introduced, a flocculant supply unit that supplies a flocculant, a solid-liquid separation unit that separates aggregates, and a flocculant from the flocculant supply unit. A plurality of coagulant addition amount adjusting devices for adjusting the addition amount of the coagulant and adding the coagulant to the aggregating reaction tank, wherein at least one of the coagulant adding amount adjusting devices is a detection means for detecting the turbidity of the treated water; Equipped with adjusting means for adjusting the coagulant addition amount based on the detection value of the means, when the detection value of the detection means is within a predetermined setting range, the amount of coagulant according to the detection value is added, And the detected value is the predetermined time T or more, the upper limit value S of the setting range
When the number exceeds 2 , the coagulant addition amount can be set to a predetermined value V 2 so that it can be set. The coagulant addition amount adjusting device can be set so that the coagulant addition amount becomes a predetermined value V 1 when the detection value of the detecting means becomes less than the setting range lower limit value S 1. .

【0010】本発明の凝集剤添加量調節装置は、被処理
水が導入される凝集反応槽と、凝集剤を供給する凝集剤
供給部と、凝集物を分離する固液分離部とを備えた水処
理装置に用いられ、凝集剤供給部からの凝集剤を添加量
調節して凝集反応槽に添加する凝集剤添加量調節装置で
あって、処理水の濁度を検出する検出手段と、検出手段
の検出値に基づいて凝集剤添加量を調節する調節手段と
を備え、検出手段の検出値が予め定めた設定範囲内にあ
るときに、検出値に応じた量の凝集剤が添加され、かつ
検出値が設定範囲の下限値S1未満となったときに、凝
集剤添加量が所定の値V1となるように設定できるよう
にされていることを特徴とする。本発明の凝集剤添加量
調節装置は、被処理水が導入される凝集反応槽と、凝集
剤を供給する凝集剤供給部と、凝集物を分離する固液分
離部とを備えた水処理装置に用いられ、凝集剤供給部か
らの凝集剤を添加量調節して凝集反応槽に添加する凝集
剤添加量調節装置であって、処理水の濁度を検出する検
出手段と、検出手段の検出値に基づいて凝集剤添加量を
調節する調節手段とを備え、検出手段の検出値が予め定
めた設定範囲内にあるときに、検出値に応じた量の凝集
剤が添加され、かつ検出値が所定時間T以上、設定範囲
の上限値S2を越えたときに、凝集剤添加量が所定値V2
となるように設定できるようにされた構成とすることが
できる。この凝集剤添加量調節装置は、検出手段の検出
値が設定範囲下限値S1未満となったときに、凝集剤添
加量が所定の値V1となるように設定できるようにする
ことができる。
The coagulant addition amount control apparatus of the present invention comprises a coagulation reaction tank into which water to be treated is introduced, a coagulant supply section for supplying a coagulant, and a solid-liquid separation section for separating coagulates. A coagulant addition amount adjusting device used for a water treatment device, which adjusts an addition amount of a coagulant from a coagulant supply unit and adds the coagulant to a coagulation reaction tank, and a detection means for detecting turbidity of treated water, Equipped with adjusting means for adjusting the coagulant addition amount based on the detection value of the means, when the detection value of the detection means is within a predetermined setting range, the amount of coagulant according to the detection value is added, Moreover, when the detected value is less than the lower limit value S 1 of the setting range, the coagulant addition amount can be set to a predetermined value V 1 . The coagulant addition amount control device of the present invention is a water treatment device including a coagulation reaction tank into which water to be treated is introduced, a coagulant supply unit that supplies a coagulant, and a solid-liquid separation unit that separates coagulates. A coagulant addition amount adjusting device for controlling the addition amount of the coagulant from the coagulant supply part and adding it to the coagulation reaction tank, the detecting means detecting the turbidity of the treated water, and the detection of the detecting means. The amount of coagulant added is adjusted based on the value, and when the detection value of the detection unit is within a predetermined setting range, the amount of the coagulant according to the detection value is added, and the detection value Exceeds the upper limit value S 2 of the set range for a predetermined time T or more, the coagulant addition amount is a predetermined value V 2
The configuration can be set so that This aggregating agent addition amount adjusting device can be set so that the aggregating agent addition amount becomes a predetermined value V 1 when the detection value of the detection means becomes less than the setting range lower limit value S 1. .

【0011】[0011]

【発明の実施の形態】図1は、本発明の水処理装置の第
1の実施形態を示す概略構成図である。図1において、
符号1は、被処理水が導入される凝集反応槽を示し、符
号2は、凝集剤を供給する凝集剤供給部を示し、符号3
は、凝集物を固液分離する沈澱槽(固液分離部)を示
し、符号4は、凝集剤供給部2からの凝集剤を添加量調
節して凝集反応槽1に添加する第1の凝集剤添加量調節
装置を示し、符号5は、凝集剤供給部2からの凝集剤を
添加量調節して凝集反応槽1に添加する第2の凝集剤添
加量調節装置を示す。図1に示す水処理装置は、図3に
示す従来の水処理装置に、第2の凝集剤添加量調節装置
5を追加した構成となっている。
FIG. 1 is a schematic configuration diagram showing a first embodiment of a water treatment device of the present invention. In FIG.
Reference numeral 1 represents a coagulation reaction tank into which water to be treated is introduced, reference numeral 2 represents a coagulant supply unit that supplies a coagulant, and reference numeral 3
Indicates a settling tank (solid-liquid separation section) for solid-liquid separation of the agglomerates, and reference numeral 4 indicates a first agglomeration for adjusting the addition amount of the aggregating agent from the aggregating agent supply unit 2 and adding it to the aggregating reaction tank 1. The reference numeral 5 denotes a second coagulant addition amount adjusting device for adjusting the addition amount of the coagulant from the coagulant supply unit 2 and adding the coagulant to the coagulation reaction tank 1. The water treatment device shown in FIG. 1 has a configuration in which a second coagulant addition amount adjusting device 5 is added to the conventional water treatment device shown in FIG.

【0012】凝集剤供給部2は、凝集剤溶液を貯留する
凝集剤貯留槽6を備えている。第1の凝集剤添加量調節
装置4は、被処理水の流量を検出する流量計(被処理水
流量検出手段)7と、被処理水の濁度を検出する濁度計
(被処理水濁度検出手段)8と、これらからの検出信号
に基づいて駆動信号を出力する制御部9と、制御部9か
らの駆動信号に基づいて、凝集剤貯留槽6からの凝集剤
溶液の流量を調節する送液ポンプ10とを備えている。
流量計7および濁度計8は、被処理水の供給経路L1に
設けられている。送液ポンプ10は、凝集剤貯留槽6か
らの凝集剤溶液を凝集反応槽1に供給する供給経路L4
に設けられている。送液ポンプ10の制御方式として
は、インバータ制御を採用できる。
The coagulant supply unit 2 has a coagulant storage tank 6 for storing the coagulant solution. The first coagulant addition amount adjusting device 4 includes a flow meter (process water flow rate detecting means) 7 for detecting the flow rate of the water to be treated and a turbidity meter (turbidity of the water to be treated) for detecting the turbidity of the water to be treated. Degree detecting means) 8, a controller 9 for outputting a drive signal based on detection signals from these, and a flow rate of the coagulant solution from the coagulant reservoir 6 based on the drive signal from the controller 9. And a liquid feed pump 10 for
The flow meter 7 and the turbidity meter 8 are provided in the feed path L1 for the water to be treated. The liquid feeding pump 10 supplies a coagulant solution from the coagulant storage tank 6 to the coagulation reaction tank 1 through a supply path L4.
It is provided in. Inverter control can be adopted as a control method for the liquid feed pump 10.

【0013】第2の凝集剤添加量調節装置5は、処理水
の濁度を検出する濁度計(処理水濁度検出手段)11
と、濁度計11からの検出信号に基づいて駆動信号を出
力する制御部12と、制御部12からの駆動信号に基づ
いて、凝集剤貯留槽6からの凝集剤溶液の流量を調節す
る送液ポンプ(調節手段)13とを備えている。濁度計
11は、処理水の排出経路L3に設けられている。送液
ポンプ13は、凝集剤貯留槽6からの凝集剤溶液を凝集
反応槽1に供給する供給経路L5に設けられている。送
液ポンプ13の制御方式としては、インバータ制御を採
用できる。
The second coagulant addition amount adjusting device 5 is a turbidimeter (treated water turbidity detecting means) 11 for detecting the turbidity of the treated water.
And a control unit 12 that outputs a drive signal based on a detection signal from the turbidimeter 11, and a transmission unit that adjusts the flow rate of the coagulant solution from the coagulant storage tank 6 based on the drive signal from the control unit 12. A liquid pump (adjusting means) 13 is provided. The turbidity meter 11 is provided in the treated water discharge path L3. The liquid feed pump 13 is provided in the supply path L5 that supplies the coagulant solution from the coagulant storage tank 6 to the coagulation reaction tank 1. Inverter control can be adopted as a control method for the liquid feed pump 13.

【0014】以下、上記水処理装置を使用した処理方法
の第1の例を説明する。供給経路L1を通して被処理水
を凝集反応槽1に導入するとともに、凝集剤貯留槽6か
らの凝集剤溶液を供給経路L4、L5を通して凝集反応
槽1に添加する。凝集反応槽1において、被処理水中の
懸濁物質等は、凝集剤により架橋、荷電中和されること
によって凝集する。凝集物は、被処理水とともに経路L
2を通して沈澱槽3に導入され、ここで沈降分離され
る。凝集物が分離された処理水は、排出経路L3を通し
て系外に排出される。
A first example of a treatment method using the above water treatment device will be described below. The water to be treated is introduced into the coagulation reaction tank 1 through the supply path L1, and the coagulant solution from the coagulant storage tank 6 is added to the coagulation reaction tank 1 through the supply paths L4 and L5. In the coagulation reaction tank 1, suspended substances and the like in the water to be treated are aggregated by being crosslinked and neutralized by charge by an aggregating agent. Aggregate is route L along with the water to be treated
It is introduced through 2 into a settling tank 3 where it is separated by settling. The treated water from which the aggregates have been separated is discharged out of the system through the discharge path L3.

【0015】凝集剤の添加量は、第1および第2の凝集
剤添加量調節装置4、5によって以下のようにして定め
られる。第1の凝集剤添加量調節装置4では、流量計7
および濁度計8によって、被処理水の流量および濁度が
検出され、検出信号が出力される。この検出信号に基づ
いて制御部9から駆動信号が出力され、この駆動信号に
応じて送液ポンプ10が駆動し、供給経路L4からの凝
集剤溶液の流量が定められる。
The addition amount of the coagulant is determined by the first and second coagulant addition amount adjusting devices 4 and 5 as follows. In the first coagulant addition amount adjusting device 4, the flowmeter 7
The turbidity meter 8 detects the flow rate and turbidity of the water to be treated and outputs a detection signal. A drive signal is output from the control unit 9 based on this detection signal, the liquid feed pump 10 is driven according to this drive signal, and the flow rate of the coagulant solution from the supply path L4 is determined.

【0016】凝集反応槽1内の被処理水中の懸濁物質等
を凝集させるのに必要最小限となる凝集剤量(最適凝集
剤量)は、凝集反応槽1内に導入される懸濁物質量に応
じた値となる。この最適凝集剤量は、通常、被処理水の
流量と濁度との積にほぼ比例する量となる。被処理水の
流量に変動がない場合には、最適凝集剤量は被処理水の
濁度にほぼ比例する量となる。また被処理水の濁度に変
動がない場合には、最適凝集剤量は被処理水の流量にほ
ぼ比例する量となる。このため、第1の凝集剤添加量調
節装置4による凝集剤の添加量の設定値は、被処理水の
流量濁度積(流量と濁度との積)、流量、濁度のうちい
ずれかの検出値に応じて(好ましくは検出値にほぼ比例
するように)定めるのが好ましい。凝集剤は、第2の凝
集剤添加量調節装置5からも添加されるため、第1の凝
集剤添加量調節装置4においては、凝集剤添加量の設定
値を、最適凝集剤量より低く、例えば最適凝集剤量の約
50%となるように定めるのが好ましい。
The minimum amount of coagulant (optimum amount of coagulant) required for aggregating the suspended solids in the water to be treated in the flocculation reaction tank 1 is the suspended solid introduced into the flocculation reaction tank 1. The value depends on the quantity. This optimum amount of coagulant is usually an amount that is approximately proportional to the product of the flow rate of the water to be treated and the turbidity. When there is no change in the flow rate of the water to be treated, the optimum amount of coagulant is an amount that is almost proportional to the turbidity of the water to be treated. Further, when the turbidity of the water to be treated does not change, the optimum amount of the coagulant is substantially proportional to the flow rate of the water to be treated. Therefore, the setting value of the addition amount of the coagulant by the first coagulant addition amount adjusting device 4 is one of the flow rate turbidity product (product of flow rate and turbidity), the flow rate, and the turbidity of the water to be treated. It is preferable to set it according to the detected value of (preferably so as to be approximately proportional to the detected value). Since the coagulant is also added from the second coagulant addition amount adjusting device 5, in the first coagulant addition amount adjusting device 4, the set value of the coagulant adding amount is lower than the optimum coagulant amount, For example, it is preferable to set it to be about 50% of the optimum amount of the coagulant.

【0017】被処理水の流量または濁度が変動した場合
には、流量計7または濁度計8における検出値が変化
し、検出値と設定値との偏差に基づいて制御部9から駆
動信号が出力され、送液ポンプ10により凝集剤溶液流
量が調節される。凝集剤添加量の制御方式としては、P
I制御、PID制御、ファジー制御などを採用すること
ができる。これによって、常時、被処理水の流量、濁度
の検出値に応じた量の凝集剤が凝集反応槽1に添加され
る。
When the flow rate or turbidity of the water to be treated fluctuates, the detection value in the flow meter 7 or the turbidity meter 8 changes, and a drive signal is sent from the control section 9 based on the deviation between the detected value and the set value. Is output, and the flow rate of the coagulant solution is adjusted by the liquid feed pump 10. The control method for the amount of coagulant added is P
I control, PID control, fuzzy control, etc. can be adopted. As a result, the aggregating agent is constantly added to the aggregating reaction tank 1 in an amount corresponding to the flow rate of the water to be treated and the detected value of turbidity.

【0018】第2の凝集剤添加量調節装置5では、濁度
計11によって処理水の濁度が検出され、検出信号が出
力される。この検出信号に基づいて制御部12から駆動
信号が出力され、この駆動信号に応じて送液ポンプ13
が駆動し、供給経路L5からの凝集剤溶液の流量が定め
られる。処理水中の懸濁物質量は、凝集反応槽1内の未
凝集の懸濁物質の量に応じた値となるため、未凝集の懸
濁物質を凝集させるのに必要な凝集剤量は、処理水濁度
に応じた値(例えば処理水濁度にほぼ比例する値)とな
る。
In the second coagulant addition amount adjusting device 5, the turbidity meter 11 detects the turbidity of the treated water and outputs a detection signal. A drive signal is output from the control unit 12 based on this detection signal, and the liquid delivery pump 13 is output according to this drive signal.
Is driven, and the flow rate of the coagulant solution from the supply path L5 is determined. Since the amount of suspended solids in the treated water will be a value according to the amount of unaggregated suspended solids in the flocculation reaction tank 1, the amount of coagulant necessary to aggregate the unaggregated suspended solids is It becomes a value corresponding to the water turbidity (for example, a value almost proportional to the treated water turbidity).

【0019】この例の処理方法において、第2の凝集剤
添加量調節装置5は、濁度計11の検出値が、予め定め
た設定範囲(S1以上)内にあるときに、検出値に応じ
た量の凝集剤が添加され、かつ検出値が設定範囲の下限
値S1未満となったときに、凝集剤添加量が所定の値V1
となるように設定される。この下限値S1は、任意の値
とすることができる。濁度計11が正常に作動する状態
にあるとき、通常、その検出値は0以上の値となるた
め、下限値S1は0とするのが好ましい。これは、故障
などにより濁度計11の検出値が0未満となった場合に
も、凝集剤の添加を行うことができるためである。
In the processing method of this example, the second coagulant addition amount adjusting device 5 sets the detected value of the turbidimeter 11 to the detected value when the detected value is within a predetermined setting range (S 1 or more). When an appropriate amount of coagulant is added and the detected value is less than the lower limit value S 1 of the setting range, the coagulant addition amount is the predetermined value V 1
Is set. The lower limit value S 1 can be any value. When the turbidimeter 11 is in a normally operating state, its detected value is usually 0 or more, and therefore the lower limit value S 1 is preferably 0. This is because the coagulant can be added even when the detected value of the turbidimeter 11 becomes less than 0 due to a failure or the like.

【0020】処理水濁度の検出値が設定範囲(S1
上)内にあるときの第2の調節装置5による凝集剤添加
量の設定値は、この検出値にほぼ比例するように定める
のが好ましい。この設定値は、凝集剤の総添加量(第1
および第2の調節装置4、5による凝集剤添加量の合
計)が最適凝集剤量にほぼ等しくなるように定めるのが
好ましい。
When the detected value of the treated water turbidity is within the set range (S 1 or more), the set value of the coagulant addition amount by the second adjusting device 5 is determined so as to be substantially proportional to this detected value. Is preferred. This set value is the total amount of coagulant added (first
And the total amount of coagulant added by the second adjusting devices 4 and 5) is preferably set to be approximately equal to the optimum coagulant amount.

【0021】処理水の濁度が変動した場合には、濁度計
11における検出値が変化し、検出値と設定値との偏差
に基づいて制御部12から駆動信号が出力され、送液ポ
ンプ13により凝集剤溶液流量が調節される。凝集剤添
加量の制御には、PI制御、PID制御、ファジー制御
などを用いることができる。これによって、常時、処理
水の濁度の検出値に応じた量の凝集剤が凝集反応槽1に
添加される。
When the turbidity of the treated water changes, the detection value in the turbidity meter 11 changes, and a drive signal is output from the control unit 12 based on the deviation between the detection value and the set value, and the liquid feed pump. The coagulant solution flow rate is adjusted by 13. PI control, PID control, fuzzy control and the like can be used to control the coagulant addition amount. As a result, the aggregating agent is constantly added to the aggregating reaction tank 1 in an amount corresponding to the detected value of the turbidity of the treated water.

【0022】濁度計11の検出値が下限値S1未満とな
ったときの凝集剤添加量の設定値であるV1は、凝集剤
の総添加量(第1および第2の調節装置4、5による凝
集剤添加量の合計)が最適凝集剤量になるべく近くなる
ように定めるのが好ましい。
[0022] V 1 detected value of the turbidimeter 11 is a set value of the flocculant amount when a lower limit value S less than 1, the total amount of coagulant (first and second adjusting device 4 It is preferable that the total amount of coagulant added according to 5) be as close as possible to the optimum amount of coagulant.

【0023】以下、第1の調節装置4による凝集剤添加
量を最適凝集剤量に対し50%とし、かつ第2の調節装
置5による凝集剤添加量を、処理水濁度検出値に比例す
る値(処理水濁度検出値が0度以上の場合)または所定
値V1(検出値が0度未満の場合)とする場合を例とし
て、処理過程を詳しく説明する。処理水濁度検出値が0
度以上である場合の第2の調節装置5による凝集剤添加
量の設定値は、凝集反応槽1内の未凝集の懸濁物質を凝
集させることができるように定める。所定値V1は、0
度より大きく、かつ最適凝集剤量の50%以下となる値
とする。
Hereinafter, the coagulant addition amount by the first adjusting device 4 is set to 50% with respect to the optimum coagulant amount, and the coagulant adding amount by the second adjusting device 5 is proportional to the treated water turbidity detection value. The process will be described in detail by taking a value (when the detected value of the treated water turbidity is 0 degree or more) or a predetermined value V 1 (when the detected value is less than 0 degree) as an example. Treated water turbidity detection value is 0
The setting value of the addition amount of the aggregating agent by the second adjusting device 5 when it is equal to or higher than the degree is determined so that the unaggregated suspended substance in the aggregating reaction tank 1 can be aggregated. The predetermined value V 1 is 0
And a value that is 50% or less of the optimum amount of the coagulant.

【0024】第1の凝集剤添加量調節装置4では、流量
計7および濁度計8からの検出値に基づいて、最適凝集
剤量の50%に相当する量の凝集剤が供給経路L4から
凝集反応槽1に添加される。濁度計11による処理水濁
度の検出値が0度以上である場合には、この検出値に基
づいて、未凝集の懸濁物質を凝集させ得る量の凝集剤
が、第2の調節装置5の供給経路L5から凝集反応槽1
に添加される。第1および第2の調節装置4、5によっ
て添加される凝集剤量の合計は、ほぼ最適凝集剤量に相
当する量となる。
In the first coagulant addition amount adjusting device 4, based on the detection values from the flow meter 7 and the turbidimeter 8, the coagulant in an amount corresponding to 50% of the optimum coagulant amount is supplied from the supply path L4. It is added to the flocculation reaction tank 1. When the detected value of the turbidity of the treated water by the turbidimeter 11 is 0 degree or more, the amount of the aggregating agent that can agglomerate the unaggregated suspended matter is based on the detected value, and the second adjusting device is used. 5 supply path L5 to agglutination reaction tank 1
Added to. The total amount of the coagulant added by the first and second adjusting devices 4 and 5 is an amount substantially equivalent to the optimum amount of the coagulant.

【0025】この例の処理方法において、濁度計11の
故障などによって検出値が0度を下回った場合には、第
2の調節装置5からの凝集剤の添加量が所定値V1(0
度より大きく、かつ最適凝集剤量の50%以下となる
値)となる。このため、濁度計11の故障などにより濁
度検出値が実際の処理水の濁度より低くなった場合で
も、凝集反応槽1への凝集剤添加量が極端に不足するこ
とを防ぐことができる。従って、濁度計11に異常が起
きた場合でも処理水質の悪化を未然に防ぐことができ
る。
In the processing method of this example, when the detected value falls below 0 degrees due to a failure of the turbidimeter 11, the addition amount of the coagulant from the second adjusting device 5 is a predetermined value V 1 (0
Value of 50% or less of the optimum amount of coagulant). Therefore, even if the turbidity detection value becomes lower than the turbidity of the actual treated water due to a failure of the turbidimeter 11, it is possible to prevent the coagulant addition amount to the coagulation reaction tank 1 from being extremely insufficient. it can. Therefore, even if an abnormality occurs in the turbidity meter 11, it is possible to prevent deterioration of the quality of treated water.

【0026】また、一般に、フィードフォワード制御
は、想定外の外乱に対する補正ができないという問題が
あり、フィードバック制御は、外乱に対する対処が遅れ
制御量が振れる場合があるという問題がある。上記水処
理装置では、被処理水の流量または濁度の検出値に基づ
いて凝集剤を添加するフィードフォワード制御を採用し
た第1の調節装置4と、処理水の濁度の検出値に基づい
て凝集剤を添加するフィードバック制御を採用した第2
の調節装置5とを併用するので、被処理水の流量や濁度
の変動に対し迅速に対処でき、しかも想定外の要因によ
り被処理水濁度が増加した場合でも、良好な処理水を得
ることができる。
Further, in general, the feedforward control has a problem that it is not possible to correct an unexpected disturbance, and the feedback control has a problem that the countermeasure against the disturbance may be delayed and the control amount may fluctuate. In the above-mentioned water treatment device, based on the first adjusting device 4 adopting the feedforward control in which the coagulant is added based on the detected value of the flow rate of the treated water or the turbidity, and the detected value of the turbidity of the treated water. 2nd which adopted the feedback control which adds the coagulant
Since it is used together with the adjusting device 5 of No. 5, it is possible to quickly deal with fluctuations in the flow rate and turbidity of the water to be treated, and even if the turbidity of the water to be treated increases due to unexpected factors, good treated water can be obtained. be able to.

【0027】次に、上記水処理装置を用いた水処理方法
の第2の例を説明する。この例の方法において、第2の
凝集剤添加量調節装置5は、濁度計11の検出値が、予
め定めた設定範囲(S2以下)内にあるときに、検出値
に応じた量の凝集剤が添加され、かつ検出値が所定時間
T以上、設定範囲上限値S2を越えた場合に、凝集剤添
加量が所定値V2となるように設定される。処理水濁度
の検出値が設定範囲(S2以下)内にあるときの凝集剤
添加量の設定値は、この検出値にほぼ比例するように定
めるのが好ましい。この設定値は、凝集剤の総添加量
(第1および第2の調節装置4、5による凝集剤添加量
の合計)が最適凝集剤量にほぼ等しくなるように定める
のが好ましい。
Next, a second example of the water treatment method using the above water treatment apparatus will be described. In the method of this example, when the detected value of the turbidimeter 11 is within a predetermined setting range (S 2 or less), the second coagulant addition amount adjusting device 5 adjusts the amount according to the detected value. When the coagulant is added and the detected value exceeds the set range upper limit value S 2 for a predetermined time T or more, the coagulant addition amount is set to the predetermined value V 2 . When the detected value of the treated water turbidity is within the set range (S 2 or less), the set value of the coagulant addition amount is preferably determined so as to be substantially proportional to the detected value. This set value is preferably determined so that the total amount of coagulant added (the total amount of coagulant added by the first and second adjusting devices 4, 5) is approximately equal to the optimum amount of coagulant.

【0028】濁度計11の検出値が、所定時間T以上、
設定範囲上限値S2未満となったときの凝集剤添加量の
設定値であるV2は、凝集剤の総添加量(第1および第
2の調節装置4、5による凝集剤添加量の合計)が最適
凝集剤量になるべく近くなるように定めるのが好まし
い。時間Tは、被処理水の性状に応じて設定するのが好
ましい。被処理水が、濁度変動の激しい表流水(河川
水、湖水)や排水(産業排水等)である場合、時間T
は、凝集剤添加点(凝集反応槽1)から検出点(濁度計
11)までの被処理水の滞留時間に対し1〜4倍(好ま
しくは2〜3倍)とするのが好適である。また被処理水
が、濁度変動が少ない3次処理水(凝集処理および活性
汚泥処理を経た排水)や井水である場合には、時間Tを
0とすることができる。
If the detected value of the turbidity meter 11 is a predetermined time T or more,
V 2 which is the set value of the coagulant addition amount when it becomes less than the setting range upper limit value S 2 is the total coagulant addition amount (the total of the coagulant addition amounts by the first and second adjusting devices 4 and 5). ) Is preferably set so as to be as close as possible to the optimum coagulant amount. The time T is preferably set according to the properties of the water to be treated. If the water to be treated is surface water (river water, lake water) or wastewater (industrial wastewater, etc.) whose turbidity changes drastically, time T
Is preferably 1 to 4 times (preferably 2 to 3 times) the residence time of the water to be treated from the coagulant addition point (aggregation reaction tank 1) to the detection point (turbidity meter 11). . When the water to be treated is tertiary treated water (wastewater that has undergone coagulation treatment and activated sludge treatment) or well water in which turbidity fluctuation is small, the time T can be set to 0.

【0029】濁度計11による処理水濁度の検出値が設
定範囲(S2以下)内にある場合には、この検出値に基
づいて、未凝集の懸濁物質を凝集させ得る量の凝集剤
が、第2の調節装置5の供給経路L5から凝集反応槽1
に添加される。
When the detected value of the turbidity of the treated water by the turbidimeter 11 is within the set range (S 2 or less), based on this detected value, the amount of agglomeration of the unaggregated suspended matter can be agglomerated. The agent is fed from the supply path L5 of the second adjusting device 5 to the aggregation reaction tank 1
Added to.

【0030】この例の処理方法において、濁度計11へ
の懸濁物質や気泡の付着等によって、濁度計11の検出
値が、所定時間T以上、上限値S2を越えた場合には、
第2の調節装置5からの凝集剤の添加量が所定値V2
なる。このため、濁度計11への懸濁物質や気泡の付着
等によって濁度検出値が実際の処理水の濁度より高くな
った場合でも、凝集反応槽1への凝集剤添加量が過剰と
なるのを防ぐことができる。従って、凝集剤の過剰添加
により処理コストが高騰するのを防ぐことができる。
In the treatment method of this example, when the detected value of the turbidimeter 11 exceeds the upper limit S 2 for a predetermined time T or more due to the adherence of suspended substances or bubbles to the turbidimeter 11, ,
The addition amount of the coagulant from the second adjusting device 5 becomes the predetermined value V 2 . Therefore, even if the turbidity detection value becomes higher than the actual turbidity of the treated water due to the adherence of suspended matter or bubbles to the turbidimeter 11, the amount of the coagulant added to the coagulation reaction tank 1 becomes excessive. Can be prevented. Therefore, it is possible to prevent the processing cost from rising due to the excessive addition of the coagulant.

【0031】次に、上記水処理装置を用いた水処理方法
の第3の例を説明する。この例の方法において、第2の
調節装置5は、濁度計11の検出値が、予め定めた設定
範囲(S1以上、S2以下)内にあるときに、検出値に応
じた量の凝集剤が添加されるように設定される。調節装
置5は、検出値が設定範囲下限値S1未満となったとき
に凝集剤添加量が所定の値V1となり、かつ検出値が所
定時間T以上、設定範囲上限値S2を越えた場合に、凝
集剤添加量が所定の値V2となるように設定される。検
出値が設定範囲(S1以上、S2以下)内にあるときの凝
集剤添加量の設定値は、検出値にほぼ比例するように定
めるのが好ましい。この設定値は、凝集剤の総添加量が
最適凝集剤量にほぼ等しくなるように定めるのが好まし
い。所定値V2と所定値V1は互いに等しい値とすること
ができる。
Next, a third example of a water treatment method using the above water treatment apparatus will be described. In the method of this example, when the detection value of the turbidity meter 11 is within a predetermined setting range (S 1 or more, S 2 or less), the second adjusting device 5 adjusts the amount according to the detection value. The coagulant is set to be added. In the adjusting device 5, when the detected value becomes less than the lower limit value S 1 of the setting range, the coagulant addition amount becomes the predetermined value V 1 , and the detected value exceeds the upper limit value S 2 of the setting range for a predetermined time T or more. In this case, the coagulant addition amount is set to a predetermined value V 2 . The set value of the coagulant addition amount when the detected value is within the set range (S 1 or more and S 2 or less) is preferably determined so as to be substantially proportional to the detected value. This set value is preferably determined so that the total amount of coagulant added is approximately equal to the optimum amount of coagulant. The predetermined value V 2 and the predetermined value V 1 may be equal to each other.

【0032】濁度計11による処理水濁度の検出値が設
定範囲(S1以上、S2以下)内にある場合には、この検
出値に基づいて、未凝集の懸濁物質を凝集させ得る量の
凝集剤が、第2の調節装置5の供給経路L5から凝集反
応槽1に添加される。
When the detected value of the turbidity of the treated water by the turbidimeter 11 is within the set range (S 1 or more and S 2 or less), the unaggregated suspended solids are aggregated based on this detected value. The amount of flocculant to be obtained is added to the flocculation reaction tank 1 from the supply path L5 of the second controller 5.

【0033】この例の処理方法において、濁度計11の
故障などによって検出値が下限値S 1(例えば0度)を
下回った場合には、第2の調節装置5からの凝集剤の添
加量が所定値V1となる。濁度計11への懸濁物質や気
泡の付着等によって、濁度計11の検出値が、所定時間
T以上、上限値S2を越えた場合には、第2の調節装置
5からの凝集剤の添加量が所定値V2となる。このた
め、濁度検出値が実際の処理水の濁度より低くなった場
合でも、凝集反応槽1への凝集剤添加量が極端に不足す
ることを防ぐことができ、しかも濁度検出値が実際の処
理水の濁度より高くなった場合でも、凝集反応槽1への
凝集剤添加量が過剰となるのを防ぐことができる。従っ
て、凝集剤の過剰添加を防止するとともに、処理水質の
悪化を未然に防ぐことができる。
In the treatment method of this example, the turbidimeter 11
The detected value is the lower limit value S due to a failure, etc. 1(For example, 0 degrees)
If it is below the range, the addition of the coagulant from the second adjusting device 5
The added amount is a predetermined value V1Becomes Suspended substances and gas to the turbidimeter 11
The value detected by the turbidity meter 11 may be changed for a certain period of time due to the adhesion of bubbles.
T or higher, upper limit S2Second adjustment device
The amount of coagulant added from 5 is the predetermined value V2Becomes others
Therefore, if the turbidity detection value becomes lower than the turbidity of the actual treated water,
Even if the amount of coagulant added to the coagulation reaction tank 1 is extremely insufficient
It is possible to prevent the turbidity detection value from actually
Even if it becomes higher than the turbidity of water,
It is possible to prevent the addition amount of the coagulant from becoming excessive. Obey
Prevent excessive addition of coagulant and improve the quality of treated water.
It can prevent the deterioration.

【0034】図2は、本発明の水処理装置の他の実施形
態を示すもので、ここに示す水処理装置は、凝集剤貯留
槽6からの凝集剤溶液を一定の流量で凝集反応槽1に供
給する凝集剤供給部14を備えている点で、図1に示す
水処理装置と異なる。凝集剤供給部14は、供給経路L
6と送液ポンプ15とを備えている。図2に示す水処理
装置は、図4に示す従来の水処理装置に、第2の凝集剤
添加量調節装置5を追加した構成となっている。
FIG. 2 shows another embodiment of the water treatment apparatus of the present invention. In the water treatment apparatus shown here, the flocculant solution from the flocculant storage tank 6 is fed at a constant flow rate to the flocculation reaction tank 1. The water treatment device shown in FIG. 1 is different from the water treatment device shown in FIG. The coagulant supply unit 14 supplies the supply path L
6 and a liquid feed pump 15. The water treatment device shown in FIG. 2 has a configuration in which a second coagulant addition amount adjusting device 5 is added to the conventional water treatment device shown in FIG.

【0035】この水処理装置では、第1の調節装置4に
よって、被処理水の流量、濁度の検出値に応じた量の凝
集剤が凝集反応槽1に添加され、かつ凝集剤供給部14
によって、一定流量で凝集剤が添加される。さらに、第
2の調節装置5において、上述の第1〜第3の例の水処
理方法と同様にして、濁度計11の検出値が予め定めた
設定範囲内にあるときに、検出値に応じた量の凝集剤が
添加され、かつ検出値が設定範囲外となったときに、所
定量(一定流量)の凝集剤が添加される。
In this water treatment device, the first adjusting device 4 adds the coagulant in an amount according to the flow rate of the water to be treated and the detected value of the turbidity to the coagulation reaction tank 1, and the coagulant supply unit 14
The coagulant is added at a constant flow rate. Further, in the second adjusting device 5, when the detection value of the turbidity meter 11 is within a predetermined setting range, the detection value is changed to the detection value in the same manner as in the water treatment methods of the above-described first to third examples. A corresponding amount of the coagulant is added, and when the detected value is out of the set range, a predetermined amount (constant flow rate) of the coagulant is added.

【0036】また、本発明の水処理装置では、警報装置
(図示略)を設け、濁度計11の検出値が下限値S1
満または上限値S2を越えたときに警報を発することが
できるようにすることもできる。これによって、濁度計
11に異常(故障、懸濁物質付着等)が生じた場合に、
これを直ちに察知することができるようになる。このた
め、迅速に対策(濁度計11の修理、洗浄等)を講じる
ことができる。従って、短時間で正常な運転に移行する
ことができる。また、第1および第2調節装置4、5の
送液ポンプ10、13は、被処理水の供給が停止した場
合に、凝集剤の供給を停止するように構成するのが好ま
しい。
Further, in the water treatment device of the present invention, an alarm device (not shown) is provided to issue an alarm when the detected value of the turbidity meter 11 is less than the lower limit value S 1 or exceeds the upper limit value S 2. You can also allow it. As a result, when an abnormality (fault, adhesion of suspended solids, etc.) occurs in the turbidimeter 11,
You will be able to detect this immediately. Therefore, it is possible to take prompt measures (repair, cleaning, etc. of the turbidity meter 11). Therefore, normal operation can be achieved in a short time. Further, it is preferable that the liquid feed pumps 10 and 13 of the first and second adjusting devices 4 and 5 be configured to stop the supply of the coagulant when the supply of the water to be treated is stopped.

【0037】図1および図2に示す水処理装置は、それ
ぞれ図3および図4に示す従来の水処理装置に第2の調
節装置5を追加した構成を有するものである。すなわ
ち、上記実施形態の水処理装置の構成は、第2の調節装
置5を既存の水処理装置に設置することによって得るこ
とができる。
The water treatment apparatus shown in FIGS. 1 and 2 has a construction in which a second adjusting device 5 is added to the conventional water treatment apparatus shown in FIGS. 3 and 4, respectively. That is, the configuration of the water treatment device of the above embodiment can be obtained by installing the second adjustment device 5 in the existing water treatment device.

【0038】[0038]

【実施例】図1に示す水処理装置を用いて、以下に示す
ように排水の凝集処理を行った。対象排水としては、製
紙工場排水(SS濃度1000mg/l)を用いた。第
1の調節装置4の凝集剤添加量設定値は、被処理水の流
量と濁度の検出値の積から算出された最適凝集剤量の約
50%となるように定めた。第2の調節装置5は、濁度
計11の検出値が、予め定めた設定範囲(S1:0度以
上、S2:100度以下)であるときに、検出値に比例
する量(最適凝集剤量に対し約50%に相当する量)の
凝集剤が添加されるように設定した。この調節装置5
は、検出値が下限値S1:0度未満となったときに凝集
剤添加量がV1:700mg/lとなり、かつ検出値が
所定時間T:120分以上、上限値S2:100度を越
えた場合に、凝集剤添加量がV2:700mg/lとな
るように設定した。なお、上記時間Tは、凝集反応槽1
から濁度計11までの被処理水の滞留時間の2倍に相当
する時間である。第2の調節装置5の制御方式(濁度計
11の検出値が上記設定範囲内にあるとき)としては、
PI制御を採用し、P値は100%、S値は0.1Sと
した。第2の調節装置5では、凝集剤添加から濁度計1
1における濁度検出までの時間を考慮して、3分間の制
御動作後、60分間のホールド動作(制御を行わない)
を繰り返すようにした。
EXAMPLES Using the water treatment apparatus shown in FIG. 1, the waste water was coagulated as shown below. As the target wastewater, wastewater from a paper mill (SS concentration 1000 mg / l) was used. The coagulant addition amount set value of the first controller 4 was set to be about 50% of the optimum coagulant amount calculated from the product of the flow rate of the water to be treated and the detected value of turbidity. When the detected value of the turbidimeter 11 is within a predetermined setting range (S 1 : 0 degrees or more and S 2 : 100 degrees or less), the second adjusting device 5 is an amount proportional to the detected value (optimum). The amount of flocculant (corresponding to about 50% of the amount of flocculant) was set to be added. This adjusting device 5
When the detected value is lower than the lower limit value S 1 : 0 degrees, the coagulant addition amount becomes V 1 : 700 mg / l, and the detected value is a predetermined time T: 120 minutes or more, the upper limit value S 2 : 100 degrees. When it exceeds the above, the addition amount of the coagulant was set to V 2 : 700 mg / l. In addition, the time T is the aggregation reaction tank 1
It is the time corresponding to twice the residence time of the water to be treated from the turbidity meter to the turbidimeter 11. As the control method of the second adjusting device 5 (when the detected value of the turbidity meter 11 is within the above setting range),
PI control was adopted, P value was 100% and S value was 0.1S. In the second adjusting device 5, the turbidimeter 1 is added from the addition of the coagulant.
Considering the time until turbidity detection in 1), hold operation for 60 minutes (no control) after control operation for 3 minutes
Was repeated.

【0039】上記水処理装置を1年間運転したところ、
期間中、濁度計11の汚れにより検出値が実際の処理水
の濁度より異常に高くなる事故が2度発生し、また試験
目的で濁度計11を2度停止させたが、全期間を通して
処理水濁度を50mg/l以下に維持することができ
た。
When the above water treatment device was operated for one year,
During the period, there were two accidents in which the detected value became abnormally higher than the turbidity of the actual treated water due to dirt on the turbidimeter 11, and the turbidimeter 11 was stopped twice for the purpose of testing. It was possible to maintain the turbidity of the treated water at 50 mg / l or less.

【0040】[0040]

【発明の効果】以上説明したように、本発明の水処理装
置は、凝集剤添加量調節装置のうち少なくとも1つが、
処理水濁度の検出値が予め定めた設定範囲内にあるとき
に、検出値に応じた量の凝集剤が添加され、かつ検出値
が設定範囲の下限値S1未満となったときに、凝集剤添
加量が所定の値V1となるように設定できるようにされ
ているので、濁度検出手段の故障などにより濁度検出値
が実際の処理水の濁度より低くなった場合でも、凝集剤
添加量が極端に不足することを防ぐことができる。従っ
て、濁度検出手段に異常が起きた場合でも処理水質の悪
化を未然に防ぐことができる。
As described above, in the water treatment device of the present invention, at least one of the coagulant addition amount adjusting devices is
When the detected value of the treated water turbidity is within a predetermined setting range, when an amount of the coagulant corresponding to the detected value is added and the detected value is less than the lower limit value S 1 of the set range, Since the coagulant addition amount can be set to a predetermined value V 1 , even if the turbidity detection value becomes lower than the actual turbidity of the treated water due to a failure of the turbidity detection means or the like, It is possible to prevent the coagulant addition amount from being extremely insufficient. Therefore, even if an abnormality occurs in the turbidity detection means, it is possible to prevent deterioration of the treated water quality.

【0041】また、凝集剤添加量調節装置を、濁度検出
値が所定時間T以上、設定範囲の上限値S2を越えたと
きに、凝集剤添加量が所定値V2となるように設定でき
るようにすることによって、濁度検出値が実際の処理水
の濁度より高くなった場合でも、凝集剤添加量が過剰と
なるのを防ぐことができる。
Further, the coagulant addition amount adjusting device is set so that the coagulant addition amount becomes the predetermined value V 2 when the turbidity detection value exceeds the upper limit value S 2 of the setting range for a predetermined time T or more. By making it possible, even when the turbidity detection value becomes higher than the actual turbidity of the treated water, it is possible to prevent the coagulant addition amount from becoming excessive.

【図面の簡単な説明】[Brief description of drawings]

【図1】 本発明の水処理装置の一実施形態を示す概
略構成図である。
FIG. 1 is a schematic configuration diagram showing an embodiment of a water treatment device of the present invention.

【図2】 本発明の水処理装置の他の実施形態を示す
概略構成図である。
FIG. 2 is a schematic configuration diagram showing another embodiment of the water treatment device of the present invention.

【図3】 従来の水処理装置の一例を示す概略構成図
である。
FIG. 3 is a schematic configuration diagram showing an example of a conventional water treatment device.

【図4】 従来の水処理装置の他の例を示す概略構成
図である。
FIG. 4 is a schematic configuration diagram showing another example of a conventional water treatment device.

【符号の説明】[Explanation of symbols]

1・・・凝集反応槽、2・・・凝集剤供給部、3・・・沈澱槽、
4・・・第1の凝集剤添加量調節装置、5・・・第2の凝集剤
添加量調節装置、11・・・濁度計(処理水濁度検出手
段)、13・・・送液ポンプ(調節手段)
1 ... Aggregation reaction tank, 2 ... Flocculant supply part, 3 ... Precipitation tank,
4 ... 1st coagulant addition amount adjustment device, 5 ... 2nd coagulant addition amount adjustment device, 11 ... Turbidimeter (process water turbidity detection means), 13 ... Liquid sending Pump (adjusting means)

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 被処理水に凝集剤を添加し、凝集物を
分離して処理水を得る水処理装置であって、 被処理水が導入される凝集反応槽と、凝集剤を供給する
凝集剤供給部と、凝集物を分離する固液分離部と、凝集
剤供給部からの凝集剤を添加量調節して凝集反応槽に添
加する複数の凝集剤添加量調節装置とを備え、 凝集剤添加量調節装置のうち少なくとも1つは、処理水
の濁度を検出する検出手段と、検出手段の検出値に基づ
いて凝集剤添加量を調節する調節手段とを備え、 検出手段の検出値が予め定めた設定範囲内にあるとき
に、検出値に応じた量の凝集剤が添加され、かつ検出値
が設定範囲の下限値S1未満となったときに、凝集剤添
加量が所定の値V1となるように設定できるようにされ
ていることを特徴とする水処理装置。
1. A water treatment apparatus for adding a coagulant to water to be treated to separate coagulates to obtain treated water, wherein a coagulation reaction tank into which the water to be treated is introduced and coagulation for supplying the coagulant are provided. The coagulant is provided with a coagulant supply unit, a solid-liquid separation unit that separates coagulants, and a plurality of coagulant addition amount control devices that control the coagulant addition amount from the coagulant supply unit and add the coagulant to the coagulation reaction tank. At least one of the addition amount adjusting devices is provided with a detecting means for detecting the turbidity of the treated water and an adjusting means for adjusting the coagulant addition amount based on the detection value of the detecting means. When the coagulant is added in an amount corresponding to the detected value when it is within the predetermined setting range, and when the detected value is less than the lower limit value S 1 of the set range, the coagulant addition amount is a predetermined value. A water treatment device characterized in that it can be set to V 1 .
【請求項2】 被処理水に凝集剤を添加し、凝集物を
分離して処理水を得る水処理装置であって、 被処理水が導入される凝集反応槽と、凝集剤を供給する
凝集剤供給部と、凝集物を分離する固液分離部と、凝集
剤供給部からの凝集剤を添加量調節して凝集反応槽に添
加する複数の凝集剤添加量調節装置とを備え、 凝集剤添加量調節装置のうち少なくとも1つは、処理水
の濁度を検出する検出手段と、検出手段の検出値に基づ
いて凝集剤添加量を調節する調節手段とを備え、 検出手段の検出値が予め定めた設定範囲内にあるとき
に、検出値に応じた量の凝集剤が添加され、かつ検出値
が所定時間T以上、設定範囲の上限値S2を越えたとき
に、凝集剤添加量が所定値V2となるように設定できる
ようにされていることを特徴とする水処理装置。
2. A water treatment apparatus for adding a coagulant to treated water to separate coagulates to obtain treated water, wherein a coagulation reaction tank into which the treated water is introduced and coagulation for supplying the coagulant are provided. The coagulant is provided with a coagulant supply unit, a solid-liquid separation unit that separates coagulants, and a plurality of coagulant addition amount control devices that control the coagulant addition amount from the coagulant supply unit and add the coagulant to the coagulation reaction tank. At least one of the addition amount adjusting devices is provided with a detecting means for detecting the turbidity of the treated water and an adjusting means for adjusting the coagulant addition amount based on the detection value of the detecting means. When the coagulant is added in an amount corresponding to the detected value when it is within the predetermined setting range, and when the detected value exceeds the upper limit S 2 of the set range for a predetermined time T or more, the coagulant addition amount Is set so as to be a predetermined value V 2 .
【請求項3】 検出手段の検出値が設定範囲下限値S1
未満となったときに、凝集剤添加量が所定の値V1とな
るように設定できるようにされていることを特徴とする
請求項2記載の水処理装置。
3. The detection value of the detection means is set range lower limit value S 1
The water treatment device according to claim 2, wherein the amount of the coagulant added can be set to a predetermined value V 1 when the amount is less than the predetermined value.
【請求項4】 被処理水が導入される凝集反応槽と、
凝集剤を供給する凝集剤供給部と、凝集物を分離する固
液分離部とを備えた水処理装置に用いられ、凝集剤供給
部からの凝集剤を添加量調節して凝集反応槽に添加する
凝集剤添加量調節装置であって、 処理水の濁度を検出する検出手段と、検出手段の検出値
に基づいて凝集剤添加量を調節する調節手段とを備え、 検出手段の検出値が予め定めた設定範囲内にあるとき
に、検出値に応じた量の凝集剤が添加され、かつ検出値
が設定範囲の下限値S1未満となったときに、凝集剤添
加量が所定の値V1となるように設定できるようにされ
ていることを特徴とする凝集剤添加量調節装置。
4. A flocculation reaction tank into which water to be treated is introduced,
It is used in a water treatment device equipped with a coagulant supply unit that supplies a coagulant and a solid-liquid separation unit that separates coagulates. The coagulant from the coagulant supply unit is added to the coagulation reaction tank by adjusting the addition amount. A coagulant addition amount adjusting device for detecting the turbidity of the treated water, and an adjusting unit for adjusting the coagulant addition amount based on the detection value of the detecting means. When the coagulant is added in an amount corresponding to the detected value when it is within the predetermined setting range, and when the detected value is less than the lower limit value S 1 of the set range, the coagulant addition amount is a predetermined value. A coagulant addition amount adjusting device, characterized in that it can be set to V 1 .
【請求項5】 被処理水が導入される凝集反応槽と、
凝集剤を供給する凝集剤供給部と、凝集物を分離する固
液分離部とを備えた水処理装置に用いられ、凝集剤供給
部からの凝集剤を添加量調節して凝集反応槽に添加する
凝集剤添加量調節装置であって、 処理水の濁度を検出する検出手段と、検出手段の検出値
に基づいて凝集剤添加量を調節する調節手段とを備え、 検出手段の検出値が予め定めた設定範囲内にあるとき
に、検出値に応じた量の凝集剤が添加され、かつ検出値
が所定時間T以上、設定範囲の上限値S2を越えたとき
に、凝集剤添加量が所定値V2となるように設定できる
ようにされていることを特徴とする凝集剤添加量調節装
置。
5. A coagulation reaction tank into which water to be treated is introduced,
It is used in a water treatment device equipped with a coagulant supply unit that supplies a coagulant and a solid-liquid separation unit that separates coagulates. The coagulant from the coagulant supply unit is added to the coagulation reaction tank by adjusting the addition amount. A coagulant addition amount adjusting device for detecting the turbidity of the treated water, and an adjusting unit for adjusting the coagulant addition amount based on the detection value of the detecting means. When the coagulant is added in an amount corresponding to the detected value when it is within the predetermined setting range, and when the detected value exceeds the upper limit S 2 of the set range for a predetermined time T or more, the coagulant addition amount There flocculant amount adjusting apparatus characterized by being to be set to a predetermined value V 2.
【請求項6】 検出手段の検出値が設定範囲下限値S1
未満となったときに、凝集剤添加量が所定の値V1とな
るように設定できるようにされていることを特徴とする
請求項5記載の凝集剤添加量調節装置。
6. The detection value of the detection means is set range lower limit value S 1
The coagulant addition amount adjusting device according to claim 5, wherein the coagulant addition amount can be set to a predetermined value V 1 when the amount is less than the predetermined value.
JP2001238176A 2001-08-06 2001-08-06 Water treatment apparatus and apparatus for adjusting quantity of flocculant to be added Withdrawn JP2003047805A (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003093806A (en) * 2001-09-27 2003-04-02 Kurita Water Ind Ltd Flocculant injection apparatus
JP2006263506A (en) * 2005-03-22 2006-10-05 Kurita Water Ind Ltd Dehydration method and device of sludge
JP2008062191A (en) * 2006-09-08 2008-03-21 Chugoku Electric Power Co Inc:The Apparatus for treatment of exhaust gas treating solution
JP2010514554A (en) * 2006-12-29 2010-05-06 オテヴェ・ソシエテ・アノニム Method and plant for treating water by ballasted flocculation and settling
KR20160088556A (en) * 2015-01-16 2016-07-26 코오롱엔솔루션 주식회사 A Chemical Injecting and Mixing Method in Water Treatment Process
JP2017202482A (en) * 2016-05-09 2017-11-16 Jfeスチール株式会社 Flocculant injection amount control method in coagulation sedimentation treatment

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003093806A (en) * 2001-09-27 2003-04-02 Kurita Water Ind Ltd Flocculant injection apparatus
JP2006263506A (en) * 2005-03-22 2006-10-05 Kurita Water Ind Ltd Dehydration method and device of sludge
JP2008062191A (en) * 2006-09-08 2008-03-21 Chugoku Electric Power Co Inc:The Apparatus for treatment of exhaust gas treating solution
JP2010514554A (en) * 2006-12-29 2010-05-06 オテヴェ・ソシエテ・アノニム Method and plant for treating water by ballasted flocculation and settling
KR20160088556A (en) * 2015-01-16 2016-07-26 코오롱엔솔루션 주식회사 A Chemical Injecting and Mixing Method in Water Treatment Process
KR101688301B1 (en) * 2015-01-16 2016-12-20 코오롱엔솔루션 주식회사 A Chemical Injecting and Mixing Method in Water Treatment Process
JP2017202482A (en) * 2016-05-09 2017-11-16 Jfeスチール株式会社 Flocculant injection amount control method in coagulation sedimentation treatment

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