JPH09290273A - Method for adjusting amount of flocculant to be added and device therefor - Google Patents

Method for adjusting amount of flocculant to be added and device therefor

Info

Publication number
JPH09290273A
JPH09290273A JP10767496A JP10767496A JPH09290273A JP H09290273 A JPH09290273 A JP H09290273A JP 10767496 A JP10767496 A JP 10767496A JP 10767496 A JP10767496 A JP 10767496A JP H09290273 A JPH09290273 A JP H09290273A
Authority
JP
Japan
Prior art keywords
rainfall
water
coagulant
addition amount
amount
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.)
Pending
Application number
JP10767496A
Other languages
Japanese (ja)
Inventor
Toshio Totoki
敏雄 十時
Yoshinao Kishine
義尚 岸根
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 JP10767496A priority Critical patent/JPH09290273A/en
Publication of JPH09290273A publication Critical patent/JPH09290273A/en
Pending legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

PROBLEM TO BE SOLVED: To adjust chemical injection quantity (an addition of a flocculant) to be adequate, even in the case that rainfall water is mixed with the water to be treated due to rainfall. SOLUTION: When the water to be treated flows in a water treating device, at first a flow rate is measured with a flow meter 1, then SS concentration is measured by an SS densitometer 2 and next a flocculant is added (injection of a chemical) from a chemical injection pump 4, and then the water flows in a sludge dehydrator or a flocculating settling basin 3 and a solid-liquid separation treatment is performed with a dehydration treatment or a settling treatment. Detection signals of the flow meter 1 and an SS densitometer 2 and signal from a rainfall detection meter 8 are inputted in an arithmetic device 6. At a rainfall time, a factor of correction (magnification) is used to multiply a chemical injection quantity at a non rainfall time by the factor to correct the chemical injection quantity.

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】本発明は凝集剤添加量調整方
法及び装置に係り、特に降雨による雨水が被処理水に混
入することがある下水処理場、工場排水処理設備、河川
水処理設備等において採用するのに好適な凝集剤添加量
調整方法と、そのための装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a coagulant addition amount adjusting method and apparatus, and particularly in a sewage treatment plant, a factory wastewater treatment facility, a river water treatment facility, etc. where rainwater due to rainfall may mix with the water to be treated. The present invention relates to a coagulant addition amount adjusting method suitable for use and an apparatus therefor.

【0002】[0002]

【従来の技術】周知の通り、下水処理場においては、生
物処理水や、又はその沈降分離処理後の汚泥等に対し凝
集剤を主として薬注ポンプにより添加し、次いで固液分
離処理している。同様の凝集分離処理は、工場排水処理
設備、河川水を工業用水として処理するための河川水処
理設備などにおいても採用されている。
As is well known, in a sewage treatment plant, a coagulant is mainly added to biologically treated water or sludge after its sedimentation and separation treatment by a chemical injection pump, and then solid-liquid separation treatment is performed. . Similar coagulation separation treatment is also adopted in factory wastewater treatment facilities, river water treatment facilities for treating river water as industrial water, and the like.

【0003】従来、この凝集剤の添加量は、凝集処理装
置に流入するSS(懸濁物質)量に比例して設定してい
る。このSS量は、流入する被処理水の水量を流量計で
測定し、SS濃度をSS濃度計で測定して、水量とSS
濃度を乗算することによって求められる。そして、得ら
れたSS量に所定の比率の薬注率、たとえば、汚泥に高
分子凝集剤を添加するときはSS量の0.2〜0.7%
程度の薬注率をかけて、薬注量を演算し、この演算結果
に対応した薬注量となるように制御信号を薬注ポンプへ
出力する。
Conventionally, the amount of the coagulant added is set in proportion to the amount of SS (suspended substance) flowing into the coagulation treatment apparatus. This SS amount is measured by measuring the amount of inflowing treated water with a flow meter and measuring the SS concentration with an SS concentration meter,
It is obtained by multiplying the density. Then, a chemical injection rate of a predetermined ratio to the obtained SS amount, for example, 0.2 to 0.7% of the SS amount when a polymer coagulant is added to sludge
The drug injection amount is calculated by multiplying the drug injection rate by a certain degree, and a control signal is output to the drug injection pump so that the drug injection amount corresponds to the calculation result.

【0004】この薬注率は、主としてSS濃度に応じて
選定される。例えば、或る下水処理場では高分子凝集剤
の薬注率を図2のように設定している。なお、被処理水
のSS濃度に対応した薬注率をこのグラフに基づいて一
義的に定める場合と、操業担当者が凝集状況をみて薬注
率を多少増または減じて設定する場合とがある。
[0006] This chemical injection rate is selected mainly depending on the SS concentration. For example, at a certain sewage treatment plant, the chemical injection rate of the polymer coagulant is set as shown in FIG. There are cases where the chemical injection rate corresponding to the SS concentration of the water to be treated is uniquely determined based on this graph, and there are cases where the operator in charge sets the chemical injection rate by slightly increasing or decreasing it depending on the aggregation status. .

【0005】図3は懸濁水を硫酸バンドによって凝集処
理し次いで沈降分離処理する場合において、SS除去率
を90%以上とするのに必要な薬注量を示すグラフであ
る。
FIG. 3 is a graph showing the amount of chemicals required to achieve an SS removal rate of 90% or more when the suspension water is subjected to a coagulation treatment with a sulfuric acid band and then to a sedimentation separation treatment.

【0006】なお、図2,3から明らかな通り、SS濃
度が薄くなるほど薬注率を高くする必要がある。逆に、
SS濃度が濃いほど薬注率は低くて済む。即ち、SSが
濃い被処理水の場合ほどSS乾燥ベースの固形分1kg
当りの凝集剤添加量は少なくて済むことになる。
As is clear from FIGS. 2 and 3, it is necessary to increase the chemical injection rate as the SS concentration decreases. vice versa,
The higher the SS concentration, the lower the drug injection rate. That is, the solid content of SS dry base is 1 kg when the water to be treated has a high SS.
The amount of coagulant added per unit can be small.

【0007】[0007]

【発明が解決しようとする課題】被処理水の性状がさほ
ど変化しない場合は、図2,3のグラフから求まる薬注
率によって薬注ポンプを制御することによりSS成分を
効率よく凝集分離処理することができるのであるが、被
処理水に雨水が混入するとこの薬注率では凝集状態が悪
化することが認められた。
When the properties of the water to be treated do not change so much, the SS component is efficiently coagulated and separated by controlling the chemical injection pump according to the chemical injection rate obtained from the graphs of FIGS. Although it is possible, it was found that when rainwater was mixed into the water to be treated, the aggregation state deteriorated at this chemical injection rate.

【0008】例えば、降雨による地表流水が生物汚泥含
有被処理水に混ざると、この地表流水中の土砂分により
被処理水中のSS濃度がかなり上昇する。SS濃度が上
がるとそれに対応して図2,3のグラフに基づき薬注率
を下げるのであるが、このように薬注率を下げても下げ
方が不十分であり、薬注過剰となり著しい発泡をひき起
こすことが認められた。
For example, when surface runoff water due to rainfall is mixed with biological sludge-containing treated water, the SS concentration in the treated water considerably rises due to the sediment content of the surface runoff water. As the SS concentration rises, the drug injection rate is correspondingly reduced based on the graphs in Figures 2 and 3. However, even if the drug injection rate is reduced, the way of lowering is insufficient, resulting in excessive drug injection and significant foaming. Was found to cause

【0009】本発明は、このような従来技術の問題点を
解消し、降雨により水が被処理水に混入する場合でも適
切な薬注量(凝集剤添加量)となるように調整する方法
を提供することを目的とする。
The present invention solves the above problems of the prior art and provides a method of adjusting the amount of chemical injection (amount of coagulant added) to an appropriate amount even when water is mixed with water to be treated due to rainfall. The purpose is to provide.

【0010】[0010]

【課題を解決するための手段】本発明の凝集剤添加量調
整方法は、被処理水に凝集剤を添加した後、固液分離処
理する凝集分離処理方法における凝集剤の添加量の調整
方法において、該被処理水に降雨による水が混入する場
合、降雨検出器を設け、降雨検出器からの降雨検出信号
に基づいて凝集剤の添加量を調整するようにしたことを
特徴とするものである。
The method for adjusting the amount of coagulant added according to the present invention is a method for adjusting the amount of coagulant added in a coagulation separation treatment method in which a coagulant is added to water to be treated and then a solid-liquid separation treatment is carried out. When the water to be treated is mixed with water due to rainfall, a rainfall detector is provided, and the addition amount of the coagulant is adjusted based on the rainfall detection signal from the rainfall detector. .

【0011】本発明の凝集剤添加量調整装置は、懸濁物
を含む被処理水に凝集剤を添加して固液分離する凝集分
離装置と、該凝集分離装置に流入する被処理水の流量を
検出する流量計と、この被処理水中の懸濁物濃度を検出
するSS濃度計と、降雨を検出する降雨検出器と、凝集
剤添加量を調整する添加量調整手段と、該添加量調整手
段に対して与える添加量信号を演算する演算器とを有
し、該演算器において、流量計およびSS濃度計からの
信号に基づき凝集剤添加量を演算し、かつ、降雨検出器
からの信号に基づき、凝集剤添加量を補正する演算を行
い、この演算結果を添加量調整手段に出力するようにし
たことを特徴とするものである。
The coagulant addition amount adjusting device of the present invention comprises a coagulating / separating device for adding a coagulant to a water to be treated containing a suspension for solid-liquid separation, and a flow rate of the water to be treated flowing into the coagulating / separating device. A flow meter for detecting, an SS concentration meter for detecting the concentration of suspended matter in the water to be treated, a rainfall detector for detecting rainfall, an addition amount adjusting means for adjusting the coagulant addition amount, and the addition amount adjustment A calculator for calculating an addition amount signal given to the means, wherein the calculator calculates the coagulant addition amount based on the signals from the flow meter and the SS concentration meter, and the signal from the rainfall detector. Based on the above, a calculation for correcting the addition amount of the coagulant is performed, and the calculation result is output to the addition amount adjusting means.

【0012】かかる本発明の凝集剤添加量調整方法及び
装置によると、降雨に対応して薬注量を制御することに
より、降雨時の薬注量が適切なものとなる。
According to the coagulant addition amount adjusting method and apparatus of the present invention, by controlling the chemical injection amount in response to rainfall, the chemical injection amount at the time of rainfall becomes appropriate.

【0013】本発明者が従来例の生物汚泥凝集分離装置
における降雨時の発泡トラブルの原因について種々検討
したところ、土砂は生物汚泥よりも脱水し易く、従って
被処理水のSSが降雨に伴う流入土砂(土泥)によって
増えた場合には、生物汚泥濃度上昇に対応した薬注量削
減幅よりもさらに削減幅を大きく(薬注量を少なく)す
べきであることが見出された。
The present inventor has conducted various studies on the causes of foaming troubles during rainfall in the conventional biological sludge flocculation / separation apparatus. As a result, soil and sand are more easily dehydrated than biological sludge, and therefore SS of treated water flows in with rain. It was found that if the amount of soil (soil) increases, the amount of reduction should be larger (the amount of chemical injection should be smaller) than the amount of reduction in the amount of chemical injection that corresponds to the increase in the concentration of biological sludge.

【0014】即ち、水処理装置の原水ピット等に降雨と
ともに土砂が入り込むと、この土砂は水処理装置の最初
沈殿池(初沈)で分離され、初沈から発生する汚泥は土
砂が含まれた分だけSS濃度が高まる。通常、汚泥処理
ではこの初沈汚泥と、生物工程からの余剰汚泥あるいは
凝集工程の汚泥が混合されて脱水されるが、土砂は比較
的脱水し易いSS分であり、最適薬注量は生物汚泥より
も低い。そこで、このように流入土砂によりSS濃度が
増加した場合には、生物汚泥のみによってSS濃度が増
加した場合よりも薬注率削減幅を大きくする。
That is, when the sediment enters the raw water pit of the water treatment equipment with rainfall, the sediment is separated in the first settling basin (first sedimentation) of the water treatment equipment, and the sludge generated from the first sedimentation contains the sediment. The SS concentration increases as much. Normally, in sludge treatment, this initial settled sludge is mixed with excess sludge from the biological process or sludge from the coagulation process to be dehydrated, but the earth and sand are SS components that are relatively easy to dehydrate, and the optimum chemical injection amount is biological sludge. Lower than. Therefore, when the SS concentration increases due to the inflowing sediment, the reduction rate of the chemical injection rate is made larger than that when the SS concentration increases only due to the biological sludge.

【0015】また、懸濁水に無機凝集剤を添加した後、
沈澱池に導入して凝集分離処理する設備の場合において
は、雨水が原水に流入するとSS濃度が低下するばかり
でなく、被処理水量増加により沈澱池の水面積負荷が増
大する。そこで、この場合には、薄くなったSS濃度に
対応した薬注量(例えば、図3から読みとられる薬注
量)よりも多目の薬注量とし、これによって大型で重質
の凝集フロックを生成させる。
After adding the inorganic coagulant to the suspension water,
In the case of a facility for introducing coagulation and separation treatment into a sedimentation basin, when rainwater flows into raw water, not only the SS concentration decreases but also the water area load of the sedimentation basin increases due to an increase in the amount of treated water. Therefore, in this case, a larger dosage than the dosage corresponding to the reduced SS concentration (for example, the dosage read from FIG. 3) is used, which results in large and heavy floc flocs. Is generated.

【0016】[0016]

【発明の実施の形態】図1は実施の形態に係る凝集剤添
加量調整方法及び装置を示す水処理装置の制御系統図で
ある。
1 is a control system diagram of a water treatment device showing a coagulant addition amount adjusting method and device according to an embodiment.

【0017】被処理水(原水又は給泥など)が水処理装
置に流入すると、まず流量計1により流量が計測され、
次いでSS濃度計2によりSS濃度が計測され、次いで
薬注ポンプ4からの凝集剤が添加(薬注)された後、汚
泥脱水機または凝集沈殿池等の固液分離処理設備3に流
入し、脱水処理又は沈降処理による固液分離処理が行わ
れる。
When the water to be treated (raw water or mud supply) flows into the water treatment device, the flow rate is first measured by the flow meter 1,
Next, the SS concentration is measured by the SS concentration meter 2, and after the coagulant from the chemical injection pump 4 is added (chemical injection), it flows into the solid-liquid separation treatment facility 3 such as a sludge dehydrator or a coagulation sedimentation tank, Solid-liquid separation treatment by dehydration treatment or sedimentation treatment is performed.

【0018】流量計1及びSS濃度計2の検出信号及び
降雨検出器8からの信号が演算器6に入力される。
The detection signals of the flow meter 1 and the SS concentration meter 2 and the signal from the rainfall detector 8 are input to the calculator 6.

【0019】生物汚泥の脱水処理の場合(上記符号3の
固液分離処理設備は汚泥脱水機となっている。凝集剤は
高分子凝集剤とされる。)を例に取ると、給泥量Q(m
3 /h)を流量計1からの信号で読みとり、給泥濃度C
(kg/m3 )をSS濃度計2からの信号で読みとる。
次いで、SS負荷量F(kgDS/h。このDSは全乾
物量である。)を給泥量Q(m3 /h)と給泥濃度C
(kg/m3 )との積すなわちF=C×Qにより求め
る。
Taking the case of dehydration treatment of biological sludge (the solid-liquid separation treatment equipment of the above reference 3 is a sludge dehydrator. The coagulant is a polymer coagulant) as an example, the amount of sludge supply Q (m
3 / h) is read by the signal from the flow meter 1, and the mud concentration C
(Kg / m 3 ) is read by the signal from the SS densitometer 2.
Next, the SS load F (kgDS / h, where DS is the total dry matter amount) is used as the mud supply amount Q (m 3 / h) and the mud concentration C.
It is determined by the product of (kg / m 3 ), that is, F = C × Q.

【0020】降雨がないときには、このF値(kgDS
/h)を図2のグラフ(なお、このグラフの内容は予め
演算器6にインプットされている。)にあてはめて薬注
率P(%/DS)を読みとり、この薬注率PとSS負荷
量Fとを乗じて薬注量を演算する。薬注される薬液濃度
(凝集剤濃度)をB(kg/m3 )とすると、薬液の添
加量A(kg/m3 )は次式の通りとなる。
When there is no rainfall, this F value (kgDS
/ H) is applied to the graph of FIG. 2 (the contents of this graph are input to the calculator 6 in advance) to read the drug injection rate P (% / DS), and the drug injection rate P and SS load are read. The amount F is multiplied to calculate the drug injection amount. Assuming that the concentration of the chemical liquid to be dosed (concentrating agent concentration) is B (kg / m 3 ), the addition amount A (kg / m 3 ) of the chemical liquid is as follows.

【0021】A=P×F/(100×B)(m3 /h) このA量が基準薬注量となるのであるが、降雨がある場
合にはこのAに0.85ないし0.9程度の補正倍率を
乗じて補正薬注量とする。なお、この倍率は現場毎の土
砂及び汚泥性状により異なるので、現場に応じた率とす
る。
A = P × F / (100 × B) (m 3 / h) This amount of A is the standard chemical injection amount, but when there is rainfall, 0.85 to 0.9 is added to this A. Multiply the degree of correction to obtain the corrected dose. Since this ratio varies depending on the soil and sludge properties at each site, the rate should be set according to the site.

【0022】このようにして演算された薬注量(非降雨
時には上記の基準薬注量A。降雨時及び降雨後所定時間
の間は補正薬注量。)を示す指示信号を添加量調整手段
としての薬注制御器5に与え、この薬注制御器が薬注量
指示信号に基づいて薬注ポンプ4を制御する。
The addition amount adjusting means is provided with an instruction signal indicating the calculated chemical injection amount (the above-mentioned reference chemical injection amount A during non-rainfall, and the corrected chemical injection amount during rain and during a predetermined time after rain). To the medicine injection controller 5, and this medicine injection controller controls the medicine injection pump 4 based on the medicine injection amount instruction signal.

【0023】このようにして、降雨に伴う土砂流入によ
るSS濃度上昇を勘案した薬注制御を行うことにより、
降雨時でも適切な凝集処理を行える。
In this way, by performing the chemical injection control in consideration of the SS concentration increase due to the inflow of sediment due to rainfall,
Appropriate aggregation treatment can be performed even during rainfall.

【0024】なお、図1の実施の形態は生物汚泥を含む
被処理水を高分子凝集剤によって凝集処理するものであ
るが、懸濁水を無機凝集剤で凝集分離する場合も同様に
して制御する。ただし、この場合は、降雨時には上記補
正率を、例えば、1.05〜1.15とする。この補正
された薬注率を用いて、上記と同様に流入全SS量に基
づき薬注量を計算する。
In the embodiment shown in FIG. 1, the water to be treated containing biological sludge is coagulated with a polymer coagulant, but the same control is performed when the suspension water is coagulated and separated with an inorganic coagulant. . However, in this case, the correction rate is set to, for example, 1.05 to 1.15 during rainfall. Using this corrected dosing rate, the dosing amount is calculated based on the total inflow SS amount in the same manner as above.

【0025】懸濁水を硫酸バンド等の無機凝集剤で凝集
分離処理するときには、図1のフローにおいて符号3の
固液分離処理設備を凝集沈殿池とした設備を用いる。そ
して、降雨により雨水が原水に流入する場合には、大
型、重質の凝集フロックが生成するように図3から求ま
る薬注率よりも薬注量を増加させる(例えば1.05〜
1.15倍とする)。このようにして大型、重質のフロ
ックを生成させることにより、雨水流入に伴う水量増大
による沈殿池水面積負荷増大に対処することができる。
When the suspension water is subjected to the coagulation separation treatment with an inorganic coagulant such as a sulfuric acid band, the solid-liquid separation treatment equipment indicated by reference numeral 3 in the flow of FIG. 1 is used as a coagulation sedimentation tank. Then, when rainwater flows into the raw water due to rainfall, the chemical injection rate is increased more than the chemical injection rate obtained from FIG. 3 so that large-sized and heavy floc flocs are generated (for example, 1.05-
1.15 times). By generating large and heavy flocs in this way, it is possible to cope with an increase in the sedimentation pond water area load due to an increase in the amount of water accompanying rainwater inflow.

【0026】このような薬注量の補正を行うには、演算
器6に接続されたキーボード等の入力手段7により、
0.85ないし0.9、又は1.05ないし1.15な
る定数を演算器6に与え、この定数を薬注量に乗算す
る。
In order to perform such correction of the chemical injection amount, an input means 7 such as a keyboard connected to the arithmetic unit 6 is used.
A constant of 0.85 to 0.9, or 1.05 to 1.15 is given to the calculator 6, and the constant is multiplied by the dose.

【0027】なお、汚泥の種類の変動等により最適薬注
率が図2,3のグラフから若干乖離するようになった場
合にも、同様に入力手段7からこの乖離を補償するよう
な定数や、あるいはグラフそのものを別のものに更新す
るようにデータを入力する。
Even when the optimum chemical injection rate deviates slightly from the graphs shown in FIGS. 2 and 3 due to variations in the type of sludge, a constant or a constant for compensating for this deviation from the input means 7 is also provided. , Or enter the data to update the graph itself to something else.

【0028】本発明において、使用する計器は、いずれ
も必要な情報が得られれば任意のものでよく、市販のも
のが利用できる。
In the present invention, any instrument may be used as long as necessary information can be obtained, and a commercially available instrument can be used.

【0029】降雨検出器としては、湿度計、雨量計、水
処理装置への流入水量を把握する流量計等が使用でき
る。
As the rainfall detector, a hygrometer, a rain gauge, a flow meter for grasping the amount of water flowing into the water treatment device, or the like can be used.

【0030】湿度計は、例えば、相対湿度98%以上の
情報が入力されたときに降雨があると判定する。雨量計
は所定雨量に達したときに降雨ありと判定する。流量計
(設置位置は、原水槽への流入部、水処理装置の任意の
位置、処理水排出部などどこでも良い。)では、通常の
変動幅を所定量超えたときを降雨ありと判定する。
The hygrometer determines that there is rainfall when, for example, information of 98% or more relative humidity is input. The rain gauge determines that there is rainfall when a predetermined amount of rainfall is reached. In the flow meter (the installation position may be anywhere such as the inflow part to the raw water tank, any position of the water treatment device, and the treated water discharge part), it is determined that there is rainfall when the normal fluctuation range exceeds a predetermined amount.

【0031】降雨の有無を判定する閾値は、凝集処理装
置が設置されている現場毎に土砂の混入するときの雨
量、希釈されて凝集効果が影響されるときの降雨量など
が変わるので、現場毎に、経験値から設定するのが好ま
しい。
The threshold value for determining the presence or absence of rainfall varies depending on the site where the aggregating apparatus is installed, such as the amount of rainfall when soil is mixed, the amount of rainfall when diluted and the agglomeration effect is affected, and so on. It is preferable to set each time from the experience value.

【0032】添加量調整手段(薬注制御器)5は、演算
器6からの出力信号(例えば、DC4〜20mA:薬注
量をこの範囲で0〜100%に指示)を受けて薬注量を
制御できるものであればよい。薬注制御器としては、薬
注モータをインバータ等で回転数を制御、モータ減速器
の回転数を制御するものが好適に用いられるが、薬注ラ
インの弁開度を調整するものであっても良い。
The addition amount adjusting means (chemical injection controller) 5 receives the output signal from the computing unit 6 (for example, DC 4 to 20 mA: the chemical injection amount is instructed to be 0 to 100% within this range) and the chemical injection amount is received. Anything that can control As the chemical-feeding controller, one that controls the number of rotations of a chemical-feeding motor with an inverter or the like and controls the number of rotations of a motor speed reducer is preferably used, but it is one that adjusts the valve opening of the chemical-feeding line. Is also good.

【0033】[0033]

【発明の効果】以上の通り、本発明の凝集剤添加量調整
方法及び装置によると、降雨により水が被処理水に混入
する場合であっても自動的に適切な薬注量となるように
制御することができる。
As described above, according to the coagulant addition amount adjusting method and apparatus of the present invention, even if water is mixed into the water to be treated due to rainfall, an appropriate chemical dosing amount can be automatically obtained. Can be controlled.

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

【図1】実施の形態を示す制御系統図である。FIG. 1 is a control system diagram showing an embodiment.

【図2】高分子凝集の薬注量を示すグラフである。FIG. 2 is a graph showing the amount of polymer aggregation to be dispensed.

【図3】硫酸バンドの薬注量を示すグラフである。FIG. 3 is a graph showing a dosage amount of a sulfuric acid band.

【符号の説明】[Explanation of symbols]

1 流量計 2 SS濃度計 3 汚泥脱水機又は凝集沈殿池等の固液分離処理設備 4 薬注ポンプ 5 添加量調整手段(薬注制御器) 6 演算器 7 入力手段 8 降雨検出器 1 Flowmeter 2 SS Concentration Meter 3 Sludge Dewatering Machine or Solid-Liquid Separation Equipment such as Coagulation Sedimentation Tank 4 Chemical Dosing Pump 5 Addition Adjusting Means (Chemical Dosing Controller) 6 Computer 7 Input Means 8 Rainfall Detector

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 被処理水に凝集剤を添加した後、固液分
離処理する凝集分離処理方法における凝集剤の添加量の
調整方法において、 該被処理水に降雨による水が混入する場合、降雨検出器
を設け、降雨検出器からの降雨検出信号に基づいて凝集
剤の添加量を調整するようにしたことを特徴とする凝集
剤添加量調整方法。
1. A method for adjusting the addition amount of a coagulant in a coagulation separation treatment method in which a coagulant is added to treated water, and then solid-liquid separation treatment is performed. A coagulant addition amount adjusting method, wherein a detector is provided, and the coagulant addition amount is adjusted based on a rainfall detection signal from the rainfall detector.
【請求項2】 懸濁物を含む被処理水に凝集剤を添加し
て固液分離する凝集分離装置と、 該凝集分離装置に流入する被処理水の流量を検出する流
量計と、 この被処理水中の懸濁物濃度を検出するSS濃度計と、 降雨を検出する降雨検出器と、 凝集剤添加量を調整する添加量調整手段と、 該添加量調整手段に対して与える添加量信号を演算する
演算器とを有し、 該演算器において、流量計およびSS濃度計からの信号
に基づき凝集剤添加量を演算し、かつ、降雨検出器から
の信号に基づき、凝集剤添加量を補正する演算を行い、
この演算結果を添加量調整手段に出力するようにしたこ
とを特徴とする凝集剤添加量調整装置。
2. An aggregating / separating device for adding a coagulant to water to be treated containing suspensions for solid-liquid separation, a flow meter for detecting the flow rate of the to-be-treated water flowing into the aggregating / separating device, An SS concentration meter for detecting the concentration of suspended solids in the treated water, a rainfall detector for detecting rainfall, an addition amount adjusting means for adjusting the addition amount of the coagulant, and an addition amount signal given to the addition amount adjusting means. And a computing unit that computes the coagulant addition amount based on the signals from the flow meter and the SS concentration meter, and corrects the coagulant addition amount based on the signal from the rainfall detector. Calculation
A coagulant addition amount adjusting device characterized in that the calculation result is output to an addition amount adjusting means.
JP10767496A 1996-04-26 1996-04-26 Method for adjusting amount of flocculant to be added and device therefor Pending JPH09290273A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10767496A JPH09290273A (en) 1996-04-26 1996-04-26 Method for adjusting amount of flocculant to be added and device therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10767496A JPH09290273A (en) 1996-04-26 1996-04-26 Method for adjusting amount of flocculant to be added and device therefor

Publications (1)

Publication Number Publication Date
JPH09290273A true JPH09290273A (en) 1997-11-11

Family

ID=14465124

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10767496A Pending JPH09290273A (en) 1996-04-26 1996-04-26 Method for adjusting amount of flocculant to be added and device therefor

Country Status (1)

Country Link
JP (1) JPH09290273A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004058026A (en) * 2002-07-31 2004-02-26 Nitto Seiko Co Ltd Apparatus for automatically switching chemical injection
WO2004103521A1 (en) * 2003-05-22 2004-12-02 Ebara Corporation Flocculaing settling device
JP2007098287A (en) * 2005-10-05 2007-04-19 Hitachi Ltd Method for controlling operation of water purifying process
CN100435904C (en) * 2003-05-22 2008-11-26 株式会社荏原制作所 Flocculaing settling device
US20110049024A1 (en) * 2009-08-31 2011-03-03 Thomas Pank Method for treating runoff water using a series of treatment sequences to remove fine pollutants and clay
JP2011078904A (en) * 2009-10-07 2011-04-21 Masanori Aritomi Polluted water treatment apparatus, and operation control method
JP2020132982A (en) * 2019-02-25 2020-08-31 住友金属鉱山株式会社 Solid-liquid separation method of nickel high-pressure leach residue
JP2021094523A (en) * 2019-12-17 2021-06-24 株式会社クボタ Learning model generator and estimation device

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004058026A (en) * 2002-07-31 2004-02-26 Nitto Seiko Co Ltd Apparatus for automatically switching chemical injection
WO2004103521A1 (en) * 2003-05-22 2004-12-02 Ebara Corporation Flocculaing settling device
CN100435904C (en) * 2003-05-22 2008-11-26 株式会社荏原制作所 Flocculaing settling device
JP2007098287A (en) * 2005-10-05 2007-04-19 Hitachi Ltd Method for controlling operation of water purifying process
US20110049024A1 (en) * 2009-08-31 2011-03-03 Thomas Pank Method for treating runoff water using a series of treatment sequences to remove fine pollutants and clay
JP2011078904A (en) * 2009-10-07 2011-04-21 Masanori Aritomi Polluted water treatment apparatus, and operation control method
JP2020132982A (en) * 2019-02-25 2020-08-31 住友金属鉱山株式会社 Solid-liquid separation method of nickel high-pressure leach residue
JP2021094523A (en) * 2019-12-17 2021-06-24 株式会社クボタ Learning model generator and estimation device

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