JPH08323109A - Flocculating and settling device - Google Patents

Flocculating and settling device

Info

Publication number
JPH08323109A
JPH08323109A JP15550995A JP15550995A JPH08323109A JP H08323109 A JPH08323109 A JP H08323109A JP 15550995 A JP15550995 A JP 15550995A JP 15550995 A JP15550995 A JP 15550995A JP H08323109 A JPH08323109 A JP H08323109A
Authority
JP
Japan
Prior art keywords
sludge
pipe
tank
precipitator
reaction tank
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
JP15550995A
Other languages
Japanese (ja)
Inventor
Hideyo Yamauchi
英世 山内
Tadashi Takadoi
忠 高土居
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 JP15550995A priority Critical patent/JPH08323109A/en
Publication of JPH08323109A publication Critical patent/JPH08323109A/en
Pending legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

PURPOSE: To efficiently perform sedimentation to obtain supernatant-treated water by completely preventing a return pipe for returning sludge from a precipitator to a reaction tank from being clogged with sludge, and thereby returning sludge in the precipitator to the reaction tank to add sludge-containing water thereto and heighten sedimentation of sludge in the precipitator. CONSTITUTION: This flocculating and settling device is provided with a reaction tank 10 for receiving raw water, returned sludge and a precipitant to react them with each other, a precipitator 14 for introducing outflow water from the reaction tank to perform solid-liquid separation to settle the reaction product and also discharging the supernatant water, a return pipe 16 for returning the settled sludge in the precipitator 14 to the reaction tank 10, and a sludge discharge pipe 26 having a sludge discharge valve and for discharging the settled sludge outside the system. The precipitator 14 is provided with a sludge concentration detecting part 23 consisting of a sludge gathering and circulating pipe 24 having an opened inlet end near the sludge interface on normal operation to gather sludge in the tank and returning the gathered sludge to the precipitator 14 and a sludge concentration meter 25 connected in midway of the circulating pipe 24, and by a signal of the sludge concentration meter 25, opening/ closing of the sludge discharge valve of the sludge discharge pipe is controlled.

Description

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

【0001】[0001]

【産業上の利用分野】この発明は、各種の汚濁物を含有
する原水に、汚濁物の成分に合った沈殿剤を反応槽で添
加、混合し、この原水を沈殿槽に導入し、固液分離して
汚濁物を沈降させ、上澄水を得る凝集沈殿装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is to add raw water containing various pollutants to a precipitating agent suitable for the components of the pollutants in a reaction tank and mix them. The present invention relates to a flocculation / sedimentation apparatus that separates and sediments contaminants to obtain supernatant water.

【0002】[0002]

【従来の技術】このような凝集、沈殿処理において、沈
殿槽で沈降した汚泥の一部を反応槽に戻すと、反応槽で
の凝集反応、析出反応の際に返送汚泥が核となり、晶析
効果等により核の表面に沈殿物が更に析出し、汚泥の緻
密化、大形化が促進されて沈降性が極めて優れた汚泥に
なる。このため、この汚泥を含む原水を沈殿槽で固液分
離すると、汚泥の濃縮が進み、高濃度になって排泥さ
れ、汚泥容量の減少、廃棄汚泥の減容化が図れる。しか
し、このような汚泥が沈殿槽内に必要以上に滞流する
と、汚泥の濃縮が進み過ぎ、排泥管や、反応槽への返送
管が汚泥で閉塞したり、沈殿槽の底の汚泥をピットに掻
き寄せて入れるレーキに過剰の負荷が加わり、故障の原
因になったりする。このトラブルを回避するため沈殿槽
から頻繁に汚泥を排出すると、濃縮されていないスラリ
ーや、水のみを排出することになり、スラリーを再濃縮
する設備が必要になる。
2. Description of the Related Art In such coagulation / precipitation treatment, if a part of the sludge settled in the settling tank is returned to the reaction tank, the returned sludge becomes a nucleus during the coagulation reaction and the precipitation reaction in the reaction tank to cause crystallization. Due to the effect and the like, a precipitate is further deposited on the surface of the core, which promotes the densification and size increase of the sludge, resulting in a sludge having an excellent settling property. For this reason, when the raw water containing this sludge is subjected to solid-liquid separation in the settling tank, the sludge is concentrated and the concentration becomes high, and the sludge is discharged to reduce the sludge capacity and the waste sludge volume. However, if such sludge stagnates more than necessary in the settling tank, the sludge is concentrated too much, and the sludge discharge pipe and the return pipe to the reaction tank are clogged with sludge, and the sludge at the bottom of the settling tank is removed. Excessive load is applied to the rake that is pulled into the pit, which may cause malfunction. If sludge is frequently discharged from the settling tank in order to avoid this trouble, only unconcentrated slurry or water will be discharged, and a facility for reconcentrating the slurry is required.

【0003】[0003]

【発明が解決しようとする課題】そこで、沈殿槽内に汚
泥がどの程度、堆積しているかを、汚泥の界面(上面)
を検出して探り、或る程度、堆積したら排泥弁を開いて
沈殿槽から汚泥を排出し、堆積量が少なくなったら排泥
弁を閉じて汚泥が堆積するのを待つという方法で排泥を
制御し、排泥管や、返送管の閉塞などのトラブルに対処
することが提案されている。しかし、汚泥の界面を検出
するには、超音波を利用した汚泥界面計を沈殿槽の液中
に吊下げたり、汚泥界面計を沈殿槽の液中に常設したり
する必要があるが、いずれにしても沈殿槽内の液は汚れ
ているため、汚泥界面計のセンサー部や発信部は汚染さ
れ、汚泥の界面を正確に検出することができなくなる。
又、汚泥界面計を液中に吊下げた場合は汚泥界面計を頻
繁に水面上に引き上げ、センサー部や発信部を清掃すれ
ばよいが、沈殿槽は一般に大型であり、汚泥界面計を液
中に沈めたり、引き上げたりする装置も大がかりにな
り、保守管理が大変な作業になる。
Therefore, how much sludge is accumulated in the settling tank is determined by the interface (upper surface) of the sludge.
The sludge is opened to a certain extent and the sludge valve is opened to discharge the sludge from the settling tank, and when the accumulated amount is small, the sludge valve is closed and the sludge is waited for to accumulate. It has been proposed to control such problems and deal with troubles such as clogging of the drainage pipe and return pipe. However, in order to detect the interface of sludge, it is necessary to suspend a sludge interfacial meter using ultrasonic waves in the liquid of the sedimentation tank, or to permanently install the sludge interfacial meter in the liquid of the sedimentation tank. However, since the liquid in the settling tank is dirty, the sensor unit and transmitter of the sludge interface meter are contaminated, and the sludge interface cannot be accurately detected.
Also, when the sludge interfacial meter is suspended in the liquid, the sludge interfacial meter should be frequently raised above the surface of the water to clean the sensor part and the transmission part. The equipment for submersion and withdrawal also becomes large-scale, and maintenance work becomes a difficult task.

【0004】[0004]

【課題を解決するための手段】本発明は、上述した問題
点を解消するためのもので、原水と、返送汚泥と、沈殿
剤とを受入れて反応させる反応槽と、反応槽からの流出
水を導入して固液分離し、反応生成物を沈降させると共
に上澄水を排出する沈殿槽と、沈殿槽の沈降汚泥を反応
槽に返送する返送管、及び排泥弁を有し、沈降汚泥を系
外に排出する排泥管を備えた凝集沈殿装置において、沈
殿槽には、その正常運転時の汚泥界面の近傍に入口端を
開口して槽内の汚泥を採取し、採取した汚泥を沈殿槽に
戻す汚泥の採取、循環管と、この採取、循環管の途中に
接続した汚泥濃度計とからなる汚泥濃度検出部を設け、
汚泥濃度計の信号により前記排泥管の排泥弁の開閉を制
御するようにしたことを特徴とする。
Means for Solving the Problems The present invention is intended to solve the above-mentioned problems, and is a reaction tank for receiving raw water, return sludge, and a precipitant to react with each other, and water flowing out from the reaction tank. Introduce the solid-liquid separation, settling the reaction product and discharging the supernatant water, and a return pipe for returning the settling sludge of the settling tank to the reaction tank, and a sludge valve, and settling sludge In a coagulation sedimentation device equipped with a sludge pipe that discharges to the outside of the system, in the sedimentation tank, open the inlet end near the sludge interface during normal operation and collect the sludge in the tank and settle the collected sludge. A sludge concentration detection unit consisting of a sludge collection pipe for collecting sludge to be returned to the tank and a sludge concentration meter connected in the middle of this collection and circulation pipe is provided.
It is characterized in that the opening and closing of the sludge discharge valve of the sludge pipe is controlled by a signal from a sludge concentration meter.

【0005】[0005]

【実施例】図示の実施例において、10は攪拌機11、
薬注装置12を有する反応槽で、汚濁物を含有する原水
が供給管13、ポンプP1 で供給される。図示の実施例
はフッ素を含有する原水を処理するため、反応槽は第
1,第2,第3の3つが直列に接続し、第1反応槽10
−1ではNaOHを薬注して原水のpHを中性にし、第
2反応槽10−2では塩化カルシウムなどのカルシウム
源を薬注してフッ素をCaF2 の不溶性化合物にし、第
3反応槽10−3では高分子凝集剤(ポリマー)を薬注
して凝集反応させる。
Embodiment In the illustrated embodiment, 10 is a stirrer 11,
In a reaction tank having a chemical injection device 12, raw water containing contaminants is supplied by a supply pipe 13 and a pump P1. In the illustrated embodiment, raw water containing fluorine is treated, so that the first, second and third reactors are connected in series, and the first reactor 10 is used.
In -1, NaOH is dosed to make the pH of the raw water neutral, and in the second reaction vessel 10-2, a calcium source such as calcium chloride is dosed to make fluorine an insoluble compound of CaF 2 , and the third reaction vessel 10-2 is used. In -3, a polymer flocculant (polymer) is dosed to cause a flocculation reaction.

【0006】第1反応槽10−1には、沈殿槽14で沈
降した汚泥が該槽の汚泥排出ピット15、返送管16、
返送ポンプP2 を経て供給され、攪拌機11の回転で均
一に混合される。
In the first reaction tank 10-1, the sludge settled in the settling tank 14 is sludge discharge pit 15 in the tank, a return pipe 16,
It is supplied through the return pump P2 and uniformly mixed by the rotation of the stirrer 11.

【0007】各反応槽内での滞流時間は数分〜数10分
であって、その間に混合と反応が行われ、反応を行った
原水は第3反応槽10−3から排出管17によって沈殿
槽14の中央部のフィードウェル18の内部に供給され
る。沈殿槽の摺鉢形底面上に沿ってレーキ19が回転
し、該底面上に沈降する汚泥を中心の排出ピット15に
掻き寄せて入れる。レーキ19の回転軸20はフィード
ウェル18の中心を貫通して支持され、モータで回転駆
動される。汚泥の沈降界面(上面)21はフィードウェ
ル18の下端よりも下である。
The dwell time in each reaction tank is several minutes to several tens of minutes, during which mixing and reaction are carried out, and the reacted raw water is discharged from the third reaction tank 10-3 through the discharge pipe 17. It is supplied to the inside of the feed well 18 at the center of the settling tank 14. The rake 19 rotates along the bottom surface of the sludge basin of the settling tank, and the sludge settling on the bottom surface is scraped into the central discharge pit 15. The rotary shaft 20 of the rake 19 is supported by penetrating the center of the feed well 18, and is rotationally driven by a motor. The sludge sedimentation interface (upper surface) 21 is below the lower end of the feed well 18.

【0008】沈殿槽内で汚泥を沈降分離した上澄水は、
沈降汚泥の界面よりも上方、例えば排出管17と同レベ
ルで槽壁に接続した排水管22から処理水として排出さ
れる。
The supernatant water obtained by settling and separating sludge in the settling tank is
It is discharged as treated water above the interface of the settled sludge, for example, from the drain pipe 22 connected to the tank wall at the same level as the discharge pipe 17.

【0009】24はポンプP3 を接続した汚泥の採取、
循環管で、その入口端24´は沈殿槽の正常運転時にお
ける汚泥の沈降界面、又はそれより若干高い位置、例え
ば、レーキ19の回転アームの上方5〜30cmの位置
に開口し、ポンプP3 の運転により入口端24´から汚
泥を吸込み、フィードウェル18内に上から供給する。
この採取、循環管にはポンプP3 の下流の沈殿槽外の位
置に汚泥濃度計25が接続してある。上記汚泥の採取、
循環管24と、汚泥濃度計25は汚泥濃度検出部23を
構成する。汚泥濃度計25は、既知の任意なもの、例え
ば超音波式濁度計、光電管式濁度計、圧力検知式濃度計
などを使用することができ、要は管24中を流れる汚泥
液の汚泥の濃度が濃いか、薄いかを把握できるものであ
ればよい。
[0009] 24 is the collection of sludge connected to the pump P3,
In the circulation pipe, its inlet end 24 'opens at the sedimentation interface of the sludge during normal operation of the sedimentation tank or at a position slightly higher than that, for example, at a position 5 to 30 cm above the rotary arm of the rake 19, and the pump P3 The sludge is sucked from the inlet end 24 ′ by the operation and supplied into the feedwell 18 from above.
A sludge concentration meter 25 is connected to the sampling and circulation pipe at a position outside the settling tank downstream of the pump P3. Collection of the above sludge,
The circulation pipe 24 and the sludge concentration meter 25 constitute a sludge concentration detection unit 23. The sludge densitometer 25 may be any known one, for example, an ultrasonic turbidimeter, a photoelectric tube turbidimeter, a pressure-sensing densitometer, etc. In short, sludge of sludge liquid flowing in the pipe 24. Anything can be used as long as it is possible to know whether the concentration of is high or low.

【0010】そして、汚泥の排出ピット15、又は図示
のように返送管16の途中に排泥弁Vを有する排泥管2
6を設け、汚泥濃度計25の信号を制御部27を介して
排泥弁Vに伝え、排泥弁の開閉を制御する。
Then, a sludge discharge pit 15 or a sludge discharge pipe 2 having a discharge valve V in the return pipe 16 as shown in the drawing.
6 is provided to transmit a signal from the sludge concentration meter 25 to the sludge discharge valve V via the control unit 27 to control the opening / closing of the sludge discharge valve.

【0011】制御の態様は次の通りである。沈殿槽の正
常運転時、汚泥の採取、循環管の入口端24´が汚泥の
界面21から上に離れているときは、汚泥の採取、循環
管に吸込まれる汚泥液の濃度は希薄で、汚泥濃度計25
は例えば数100mg/立を示し、このときは排泥弁V
を閉に保つ。汚泥の界面が上昇し、入口端24´に達す
ると、濃度の高い汚泥液が吸込まれることになり、汚泥
濃度計は、濃縮度にもよるが、例えば数1000〜数十
万mg/立を示し、このときは排泥弁Vを開にする。こ
れによって沈殿槽内の汚泥は排泥管26から排出され、
汚泥の界面21は下がる。そして、汚泥の界面が下が
り、採取、循環管に吸込まれる汚泥液の濃度が元の状態
(例えば数100mg/立)になると排泥弁を閉じる。
The mode of control is as follows. During normal operation of the settling tank, when the sludge is collected and the inlet end 24 'of the circulation pipe is located above the interface 21 of the sludge, the sludge is collected and the concentration of the sludge liquid sucked into the circulation pipe is low. Sludge concentration meter 25
Indicates, for example, several hundred mg / stand. At this time, the sludge valve V
Keep closed. When the sludge interface rises and reaches the inlet end 24 ', a high concentration of sludge liquid is sucked in, and the sludge densitometer measures, for example, several thousand to several hundred thousand mg / liter, depending on the concentration. And the mud discharge valve V is opened at this time. As a result, the sludge in the settling tank is discharged from the sludge pipe 26,
The sludge interface 21 goes down. Then, when the sludge interface is lowered and the concentration of the sludge liquid collected and sucked into the circulation pipe becomes the original state (for example, several 100 mg / stand), the sludge discharge valve is closed.

【0012】この場合、排泥弁を連続的に開の状態にす
ると、汚泥の界面が急速に低下し、界面上の上澄水まで
が排泥管から排出される。このため制御部27にタイマ
ーを組込み、汚泥濃度計25から排泥弁を開にする指令
があったとき、制御部はタイマーによって排泥弁を小刻
みに断続的に開にし、汚泥の界面の急速な低下、上澄水
の排出を防止することが望ましい。
In this case, when the mud discharge valve is continuously opened, the interface of the sludge is rapidly lowered, and the supernatant water on the interface is discharged from the mud pipe. For this reason, a timer is incorporated in the control unit 27, and when there is a command from the sludge concentration meter 25 to open the sludge valve, the control unit opens the sludge valve intermittently by the timer, and the sludge interface is rapidly opened. It is desirable to prevent the deterioration and clearing of clear water.

【0013】図2は、汚泥の採取、循環管に接続した小
型の密閉状の検出室28の相対向した内壁面に発信部2
9と受信部30を設け、室内を流れる汚泥液の懸濁物の
量による光、超音波等の透過量、或いは反射量の変化で
濃度を知るようにした汚泥の濃度計で、この室には弁で
開閉できる洗浄水の入口と出口31a,31bを設け、
定期的に洗浄水を流し、発信部や受信部に付着する汚れ
を除去できるようにしておくとよい。又、この検出室2
8を汚泥の採取、循環管に着脱自在に設け、定期的に取
外して汚れ度を確認してもよい。更にこの検出室や、汚
泥の採取、循環管の一部を透明部材で形成することによ
り、汚泥の濃度の変化を目視し、汚泥濃度計の検出結果
を確認にすることができる。
FIG. 2 shows the transmitting portion 2 on the inner wall surfaces of a small closed detection chamber 28 connected to a sludge collection and circulation pipe, which face each other.
9 and a receiver 30 are provided, and a sludge densitometer for detecting the concentration of a suspended sludge liquid flowing in the room by changing the amount of light or ultrasonic waves transmitted or reflected, Has an inlet and outlet 31a, 31b for washing water that can be opened and closed with a valve,
It is advisable to flush the cleaning water regularly so that the dirt attached to the transmitter and the receiver can be removed. Also, this detection chamber 2
8 may be detachably provided in the sludge collection and circulation pipes and periodically removed to check the degree of contamination. Furthermore, by forming the detection chamber, sludge collection, and part of the circulation pipe with a transparent member, changes in the sludge concentration can be visually checked and the detection result of the sludge concentration meter can be confirmed.

【0014】又、図3に示すように汚泥の採取、循環管
に、小形の開放容器32を接続し、この容器内の相対向
した壁面に発信部29と受信部30を設け、図2と同様
に汚泥の濃度を知るようにしてもよい。この場合は開放
式であるため発信部や受信部の汚れの状況が目視で把握
できると共に、洗浄も容易に行える。
Further, as shown in FIG. 3, a small open container 32 is connected to the sludge collection and circulation pipe, and a transmitting part 29 and a receiving part 30 are provided on the opposite wall surfaces in this container, as shown in FIG. Similarly, the sludge concentration may be known. In this case, since it is an open type, it is possible to visually check the state of contamination of the transmitting unit and the receiving unit and to easily perform cleaning.

【0015】図1の凝集沈殿装置によりフッ素濃度10
00〜2000mg/立の原水を処理した。約1週間で
汚泥濃度は400〜500g/立に上昇した。排泥弁V
を閉に保ったまゝ運転を継続した所、約1ケ月後に返送
管と、排泥管に閉塞が起きた。これは沈殿槽の沈降汚泥
を反応槽に戻して循環させる循環法では、沈殿槽に生成
する汚泥の沈降性が極めて良好であるため、沈殿槽内に
汚泥が溜り過ぎると、必要以上の濃縮が起きることが原
因であると推定される。
Fluorine concentration of 10 with the coagulation-sedimentation apparatus of FIG.
100 to 2000 mg / liter of raw water was treated. The sludge concentration increased to 400 to 500 g / stand in about one week. Sludge valve V
When the operation was continued while keeping the valve closed, the return pipe and the mud pipe were clogged about one month later. This is because in the circulation method in which the settling sludge in the settling tank is returned to the reaction tank and circulated, the settling property of the sludge generated in the settling tank is extremely good, so if the sludge accumulates too much in the settling tank, it will be concentrated more than necessary. It is presumed that the cause is the occurrence.

【0016】これに対し、汚泥の界面が上昇し、汚泥濃
度計25が10000mg/立になる都度、排泥弁Vを
開にして汚泥を排泥管26から排出し、汚泥濃度計が5
00mg/立になると排泥弁を閉じると、3ケ月間連続
運転を行っても返送管や排泥管に閉塞は生じなかった。
On the other hand, every time the sludge interface rises and the sludge concentration meter 25 reaches 10000 mg / stand, the sludge valve V is opened and the sludge is discharged from the sludge pipe 26.
When the mud discharge valve was closed at 00 mg / stand, no blockage occurred in the return pipe or the mud pipe even after continuous operation for 3 months.

【0017】[0017]

【発明の効果】以上で明らかなように、本発明によれば
沈殿槽から反応槽に汚泥を返送する返送管や、汚泥を排
出する排泥管の管内で汚泥が詰るのを完全に防止でき、
これにより沈殿槽内の汚泥を反応槽に返送して汚濁物含
有水に混合し、沈殿槽での汚泥の沈降性を高め、効率よ
く沈降分離を行い、上澄処理水を得ることができる。
As is apparent from the above, according to the present invention, it is possible to completely prevent clogging of sludge in the return pipe for returning sludge from the settling tank to the reaction tank and the sludge discharge pipe for discharging sludge. ,
Thereby, the sludge in the settling tank is returned to the reaction tank and mixed with the water containing pollutants, the sedimentation property of the sludge in the settling tank is enhanced, and the sludge is efficiently separated to obtain the supernatant treated water.

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

【図1】本発明の凝集沈殿装置の一実施例のフローシー
トである。
FIG. 1 is a flow sheet of an embodiment of a coagulating sedimentation device of the present invention.

【図2】汚泥濃度計の第1例の断面図である。FIG. 2 is a sectional view of a first example of a sludge concentration meter.

【図3】汚泥濃度計の第2例の断面図である。FIG. 3 is a sectional view of a second example of a sludge concentration meter.

【符号の説明】[Explanation of symbols]

10 反応槽 11 攪拌機 12 薬注装置 13 供給管 14 沈殿槽 15 汚泥排出ピット 16 汚泥の返送管 17 排出管 18 フィードウェル 19 レーキ 20 レーキの回転軸 21 汚泥の沈降界面 22 排水管 23 汚泥濃度検出部 24 汚泥の採取、循環管 25 汚泥濃度計 26 排泥管 27 制御部 28 汚泥濃度計の検出室 29 発信部 30 受信部 32 汚泥濃度計の開放容器 10 Reaction Tank 11 Stirrer 12 Chemical Injection Device 13 Supply Pipe 14 Sedimentation Tank 15 Sludge Discharge Pit 16 Sludge Return Pipe 17 Discharge Pipe 18 Feedwell 19 Rake 20 Rake Rotation Shaft 21 Sludge Sedimentation Interface 22 Drainage Pipe 23 Sludge Concentration Detector 24 Sludge collection and circulation pipe 25 Sludge concentration meter 26 Exhaust pipe 27 Control section 28 Sludge concentration meter detection room 29 Transmitting section 30 Receiver section 32 Sludge concentration meter open container

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 原水と、返送汚泥と、沈殿剤とを受入れ
て反応させる反応槽と、反応槽からの流出水を導入して
固液分離し、反応生成物を沈降させると共に上澄水を排
出する沈殿槽と、沈殿槽の沈降汚泥を反応槽に返送する
返送管、及び排泥弁を有し、沈降汚泥を系外に排出する
排泥管を備えた凝集沈殿装置において、沈殿槽には、そ
の正常運転時の汚泥界面の近傍に入口端を開口して槽内
の汚泥を採取し、採取した汚泥を沈殿槽に戻す汚泥の採
取、循環管と、この採取、循環管の途中に接続した汚泥
濃度計とからなる汚泥濃度検出部を設け、汚泥濃度計の
信号により前記排泥管の排泥弁の開閉を制御するように
したことを特徴とする凝集沈殿装置。
1. A reaction tank for receiving raw water, returned sludge, and a precipitating agent to react with each other, and introducing outflow water from the reaction tank for solid-liquid separation to precipitate a reaction product and discharge supernatant water. In the coagulating sedimentation device having a settling tank that performs the above, a return pipe that returns settling sludge from the settling tank to the reaction tank, and a sludge discharge valve, and a sludge pipe that discharges the settling sludge to the outside of the system, , Open the inlet end near the sludge interface during normal operation, collect the sludge in the tank, and return the collected sludge to the settling tank. A sludge concentration detector comprising the above sludge concentration meter, and the opening and closing of the sludge discharge valve of the sludge pipe is controlled by the signal of the sludge concentration meter.
JP15550995A 1995-05-31 1995-05-31 Flocculating and settling device Pending JPH08323109A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15550995A JPH08323109A (en) 1995-05-31 1995-05-31 Flocculating and settling device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15550995A JPH08323109A (en) 1995-05-31 1995-05-31 Flocculating and settling device

Publications (1)

Publication Number Publication Date
JPH08323109A true JPH08323109A (en) 1996-12-10

Family

ID=15607612

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15550995A Pending JPH08323109A (en) 1995-05-31 1995-05-31 Flocculating and settling device

Country Status (1)

Country Link
JP (1) JPH08323109A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012509170A (en) * 2008-11-19 2012-04-19 セバーン トレント デ ノラ,エルエルシー Marine sewage treatment
JP2018143914A (en) * 2017-03-01 2018-09-20 オルガノ株式会社 Flocculation sedimentation apparatus and driving method thereof
CN112807759A (en) * 2020-12-28 2021-05-18 安徽国祯环保节能科技股份有限公司 Uniform sludge discharge system for secondary sedimentation tank of sewage treatment plant and control method thereof

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012509170A (en) * 2008-11-19 2012-04-19 セバーン トレント デ ノラ,エルエルシー Marine sewage treatment
JP2018143914A (en) * 2017-03-01 2018-09-20 オルガノ株式会社 Flocculation sedimentation apparatus and driving method thereof
CN112807759A (en) * 2020-12-28 2021-05-18 安徽国祯环保节能科技股份有限公司 Uniform sludge discharge system for secondary sedimentation tank of sewage treatment plant and control method thereof

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