JP5473560B2 - Water purification automatic continuous monitoring device and continuous water purification system monitoring system using the same - Google Patents

Water purification automatic continuous monitoring device and continuous water purification system monitoring system using the same Download PDF

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JP5473560B2
JP5473560B2 JP2009269508A JP2009269508A JP5473560B2 JP 5473560 B2 JP5473560 B2 JP 5473560B2 JP 2009269508 A JP2009269508 A JP 2009269508A JP 2009269508 A JP2009269508 A JP 2009269508A JP 5473560 B2 JP5473560 B2 JP 5473560B2
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悟 土井
治美 能登
健次郎 石垣
和夫 服部
紀子 森垣
裕司 高橋
一布 落合
博美 鈴木
斎藤  弘
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ISOMURA HOSUI KIKO KABUSHIKI KAISHA
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本発明は、浄水場の浄水プロセスの水質監視・制御システムに関するものであり、特に浄水場における水処理全般の危機管理に関するものである。   The present invention relates to a water quality monitoring / control system for a water purification process of a water purification plant, and more particularly to crisis management of water treatment in general at a water purification plant.

一般に、浄水場では河川や貯水池などの水源から原水を取水し、凝集、フロック形成、沈殿、ろ過および殺菌の単位プロセスを経て、被処理水から懸濁質とコロイド質を除去し、細菌等を無害化し、水道水として供給している。
上記のように、浄水処理においては、凝集沈殿処理とろ過処理とを組み合わせて行う方法が広く採用されている。
浄水場の一般的な水処理フローでは、混和池で凝集剤等の水処理薬剤が注入され、急速攪拌機等で攪拌および混合された後、後段のフロック形成池、薬品沈殿池、急速ろ過池を経て、処理水の濁度は厚生労働省が非特許文献1で指導している0.1度以下にまで制御される。上記フローの全所要時間(全滞留時間)は通常6時間程度である。
In general, water treatment plants take raw water from water sources such as rivers and reservoirs, pass through unit processes of coagulation, flock formation, sedimentation, filtration and sterilization to remove suspended solids and colloids from the treated water and remove bacteria, etc. It is detoxified and supplied as tap water.
As described above, in the water purification treatment, a method of combining the coagulation sedimentation treatment and the filtration treatment is widely adopted.
In a general water treatment flow in a water purification plant, a water treatment chemical such as a flocculant is injected in a mixing pond, stirred and mixed with a rapid stirrer, etc., and then passed through a flock formation pond, a chemical sedimentation pond, and a rapid filtration pond. After that, the turbidity of the treated water is controlled to 0.1 degrees or less that the Ministry of Health, Labor and Welfare teaches in Non-Patent Document 1. The total required time (total residence time) of the flow is usually about 6 hours.

最近、全国各地の水道水源では富栄養化に起因する微小プランクトンの大発生が頻発している。微小プランクトンは、急速ろ過池より漏出してろ過水濁度を0.1度以上に上昇させる原因となるので、水道事業体ではその処理対策に苦慮しているところである。
厚生労働省は水道水を介して発生したクリプトスポリジウムによる感染症への対応として、ろ過水濁度0.1度以下管理(非特許文献1参照)を指導しているため、各地の水道事業者はろ過水濁度の常時0.1度以下管理を最も重要な水質管理項目と位置づけている。
Recently, there have been frequent outbreaks of microplankton due to eutrophication in tap water sources throughout the country. Since microplankton leaks from the rapid filtration pond and increases the turbidity of the filtered water to 0.1 ° C. or more, the water utility is struggling to take countermeasures.
The Ministry of Health, Labor and Welfare is instructing management of filtered water turbidity of 0.1 degrees or less (see Non-Patent Document 1) as a response to infection caused by cryptosporidium generated through tap water. Management of filtered water turbidity at or below 0.1 degrees is positioned as the most important water quality management item.

ところが、現在の科学的知識では微小プランクトンの発生を事前予知することは不可能であるため、水道事業者はろ過水の濁度変化を昼夜連続で監視して、ろ過水濁度が上昇した時点で、初めて前凝集剤強化や後凝集剤注入などの対応をとるのみであった。
このような現場の対応では時間遅れが生ずるため、水道事業者はより安全側の対応として、ろ過水濁度の小さな動きをもとに予防措置として凝集強化などの対応措置を取っているのが現状である。
However, because current scientific knowledge cannot predict the occurrence of microplankton in advance, the water utility monitors the turbidity change of the filtered water continuously day and night, and when the filtered water turbidity increases. For the first time, only measures such as strengthening the pre-flocculating agent and injecting the post-flocculating agent were taken.
Since time delays occur in such on-site responses, water utilities are taking safety measures such as cohesion strengthening as a precautionary measure based on the small movement of filtered water turbidity. Currently.

しかしながら、このような対応は凝集剤の非合理的な大量注入をもたらす上に、特に夜間では判断時間の遅れに伴うろ過水濁度漏洩事故の原因ともなっているので、水道事業者の大きな悩みのひとつともなっている。
これらの問題を解決するために、連続式ジャーテスタを用いて、高分子凝集剤を用いたフロック形成池後の水質に相当する処理水を測定し、その結果に基づき便宜的に対応する方法が提案されている(特許文献1)。
However, such a response causes an irrational mass injection of the flocculant and also causes a filtered water turbidity leak accident caused by a delay in judgment time, especially at night. It is also.
In order to solve these problems, a continuous jar tester is used to measure treated water corresponding to the water quality after the floc formation pond using the polymer flocculant, and there is a method for convenient handling based on the results. It has been proposed (Patent Document 1).

しかし、実施設の水質評価テストでは、上記の高分子凝集剤を用いた処理だけでなく、ろ過処理まで行なって評価することが必要とされている。
ところが、小型化した急速ろ過カラムの製作は、ろ過層の支持、ろ過層周囲に沿った短絡流の防止などの点で各種の問題があり、実施設のろ過装置を模擬することが困難であることから、それに変わる方法もいくつか提案されている(特許文献2〜4)。
しかしながら、これらの従来の方法は、ろ過処理後の水質を測定するものではないことから、実施設の急速ろ過池で処理された後のろ過水濁度に十分に対応するものではなく、依然として満足のできる監視方法ではなかった。
However, in the water quality evaluation test of the implementation facility, it is necessary to evaluate not only the treatment using the polymer flocculant but also the filtration treatment.
However, the production of a miniaturized rapid filtration column has various problems in terms of supporting the filtration layer and preventing short-circuit flow along the periphery of the filtration layer, and it is difficult to simulate the filtration device of the implementation. For this reason, several methods have been proposed (Patent Documents 2 to 4).
However, since these conventional methods do not measure the water quality after filtration, they do not sufficiently correspond to the filtered water turbidity after being treated in the rapid filtration basin of the implementation facility, and are still satisfactory. It was not possible to monitor.

特開昭63−162007号公報JP 63-162007 A 特開2002−253904号公報JP 2002-253904 A 特開昭54−93848号公報JP 54-93848 A 特開平5−146608号公報JP-A-5-146608

厚生労働省告示「水道におけるクリプトスポリジウム等対策指 針」(平成19年)Ministry of Health, Labor and Welfare Notification “Cryptosporidium Guidelines for Water Supply” (2007)

本発明の連続式監視装置は、実施設の浄水設備におけるフロック形成池以降の機能を全て備え、且つ、その設備を小型化したものであり、ろ過水濁度を測定するまでの時間を実施設の1/6から1/12程度に相当する1時間から30分以内とするものであり、そこで得られた結果をもとに、実施設のろ過水濁度の変化を5時間以上前に予知し、凝集強化のタイミングを適正化することで、実施設での対応遅れの解消を課題とするものである。   The continuous monitoring device of the present invention has all the functions after the floc formation pond in the water purification facility of the implementation, and the facility has been miniaturized, and the time until measurement of filtered water turbidity is implemented. 1/6 to 1/12 of 1 hour to 30 minutes or less, and based on the results obtained there, the change in filtered water turbidity of the implementation facility is predicted more than 5 hours ago However, by optimizing the timing of cohesion strengthening, the problem is to eliminate the delay in response at the implementation facility.

すなわち、本発明は、実施設の浄水設備におけるフロック形成池以降の設備を小型化した、フロック形成池ユニット、傾斜板沈降装置付き薬品沈殿池ユニット、急速ろ過池ユニット及び濁度監視ユニットを有する浄水処理自動連続式監視装置であり、フロック形成池ユニット及び傾斜板付き薬品沈殿池ユニットまでの滞留時間を20分程度とし、急速ろ過池ユニットを含めた全滞留時間を30分から1時間程度以内(濁度測定を含む)とすることを可能とした監視装置である。   That is, the present invention is a purified water having a floc formation pond unit, a chemical sedimentation basin unit with an inclined plate settling device, a rapid filtration basin unit, and a turbidity monitoring unit in which the equipment after the floc formation pond in the water purification facility of the implementation is miniaturized. This is an automatic continuous monitoring system. The residence time to the floc formation pond unit and the chemical sedimentation basin unit with inclined plate is about 20 minutes, and the total residence time including the rapid filtration basin unit is about 30 minutes to less than 1 hour (turbidity) Monitoring device).

フロック形成からろ過までの全滞留時間を1時間以内とすることを可能にするためには、既存の凝集、フロック形成、沈殿装置の改良と併せて、機能を損なうことのない小型ろ過装置の開発が課題となり、本発明はそれらの各課題を解決することにより完成したものである。また、本発明の連続式監視装置を用いることにより、水質変化に迅速に対応可能な浄水プロセスの連続制御システムを完成したものである。   In order to make the total residence time from floc formation to filtration within 1 hour, the development of a small filtration device that does not impair the function, in addition to the improvement of the existing agglomeration, floc formation and sedimentation equipment The present invention has been completed by solving each of these problems. Moreover, the continuous control system of the water purification process which can respond rapidly to a water quality change is completed by using the continuous monitoring apparatus of this invention.

本発明の浄水処理自動連続式監視装置は、実施設の浄水設備におけるフロック形成池以降の機能を全て備え、且つ、その設備を小型化した、フロック形成池ユニット、傾斜板沈降装置付き薬品沈殿池ユニット、急速ろ過池ユニット並びに沈殿水及びろ過水の濁度監視ユニットを有する浄水処理自動連続式監視装置であって、フロック形成からろ過までの水処理所要時間を実施設の1/6から1/12程度に短縮することにより浄水処理状態を早期に監視できるものである(請求項1の発明)。   The water purification automatic continuous monitoring device of the present invention has all the functions after the floc formation pond in the water purification facility of the implementation, and the equipment is downsized. A water purification treatment automatic continuous monitoring apparatus having a unit, a rapid filtration pond unit, and a turbidity monitoring unit for precipitated water and filtrate. The time required for water treatment from flock formation to filtration is 1/6 to 1 / By shortening to about 12, the state of the water purification treatment can be monitored at an early stage (invention of claim 1).

本発明の浄水処理自動連続式監視装置における傾斜板沈降装置付き薬品沈殿池ユニットは、傾斜板沈降装置、沈殿槽及び迂流壁を備えた越流槽とからなり、傾斜板沈降装置部分の傾斜板ピッチが異なる傾斜板沈降装置と交換可能であり、沈殿槽がその底部に自動排泥装置を有すると共に、下部の汚泥溜りに汚泥流出防止用阻流装置を有し、越流槽の迂流壁の上部を滑らかな傾斜構造にすることにより、沈殿水の濁度を1.0度未満とするものである(請求項2の発明)。   The chemical sedimentation basin unit with an inclined plate settling device in the automatic continuous monitoring system for water purification treatment of the present invention comprises an inclined plate settling device, a settling tank, and an overflow tank equipped with a bypass wall, and an inclined plate settling device portion is inclined. It can be exchanged with an inclined plate settling device with a different plate pitch, and the settling tank has an automatic mud discharge device at the bottom, and a sludge preventive device for sludge outflow prevention at the bottom sludge reservoir, bypassing the overflow tank By making the upper part of the wall a smooth inclined structure, the turbidity of the precipitated water is less than 1.0 degree (invention of claim 2).

本発明の浄水処理自動連続式監視装置における急速ろ過池ユニットは、小型ろ過カラムであり、カスケード方式での導水により引き起こされる不陸を解消するための不陸防止用阻流装置が上部に設けられ、ろ過層を支持する固定支持板が下部に設けられている。
さらに、時間設定又は水位計の水位設定に基づく自動洗浄機能を有し、ろ過水の濁度を0.05度以下とするものである(請求項3の発明)。
The rapid filtration pond unit in the automatic continuous monitoring system for water purification treatment of the present invention is a small filtration column, and is provided with a non-land prevention baffle for eliminating unevenness caused by water introduction in cascade. A fixed support plate for supporting the filtration layer is provided in the lower part.
Furthermore, it has an automatic washing function based on the time setting or the water level setting of the water level meter, and the turbidity of the filtered water is set to 0.05 degrees or less (invention of claim 3).

本発明の浄水処理自動連続式監視装置は、フロック形成池ユニット、傾斜板沈降装置付き薬品沈殿池ユニット及び急速ろ過池ユニットが、透明材料で形成されており、外部から各ユニット内部の状態が目視観察可能な構造である(請求項4の発明)。
本発明の浄水処理自動連続式監視装置におけるフロック形成池ユニットは、複数の攪拌機を有し、それらの攪拌機は原水の水質変化に応じて互いに独立して回転速度の調整が可能である(請求項5の発明)
The water purification treatment automatic continuous monitoring device of the present invention has a floc formation pond unit, a chemical sedimentation basin unit with an inclined plate settling device and a rapid filtration basin unit formed of a transparent material, and the state inside each unit is visually observed from the outside. This is an observable structure (the invention of claim 4).
The floc formation pond unit in the water purification automatic continuous monitoring apparatus of the present invention has a plurality of agitators, and these agitators can adjust the rotation speed independently of each other according to the water quality change of the raw water (claims) (5 invention)

本発明の浄水処理自動連続式監視装置における濁度監視ユニットは、濁度計又は濁度計及び微粒子カウンターを備えるものであり、これらの濁度計等により沈殿水及びろ過水の濁度監視を行なうものである(請求項6の発明)。
本発明の浄水プロセスの連続式監視装置は、上記1〜6のいずれかの浄水処理自動連続式監視装置並びにその前段階の凝集剤、塩素剤、粉末活性炭を含む薬品注入設備ユニット、急速攪拌機を装備した混和池ユニット及び濁度計、残留塩素計を含む水質計器を具備する水質監視ユニットからなり、実施設の浄水設備の機能をすべて備え、且つ、その設備を小型化し、原水の取水からろ過までの全浄水プロセス所要時間を実施設の1/6から1/12程度に短縮することにより浄水処理状態を早期に監視できるものである(請求項7の発明)。
The turbidity monitoring unit in the water purifying automatic continuous monitoring device of the present invention is provided with a turbidimeter or a turbidimeter and a fine particle counter. (Invention of claim 6)
The continuous monitoring device of the water purification process of the present invention comprises the water purification automatic continuous monitoring device of any one of 1 to 6 above, a chemical injection equipment unit including a flocculant, a chlorine agent, powdered activated carbon, and a rapid stirrer in the preceding stage. It consists of a water mixing unit and a water quality monitoring unit equipped with a water quality meter including a turbidity meter and a residual chlorine meter. It is equipped with all the functions of the water purification facility at the facility, and the facility is downsized and filtered from the intake of raw water. The water purification treatment state can be monitored at an early stage by shortening the time required for the entire water purification process from 1/6 to 1/12 of the implementation facility (invention of claim 7).

本発明の浄水プロセスの連続制御システムは、上記1〜6のいずれかの浄水処理自動連続式監視装置から得られた沈殿水濁度及びろ過水濁度の情報に基づき、浄水処理不良原因が微小プランクトンによるろ過障害か否かを判断し、微小プランクトンによるろ過障害と判断された時に、実施設の後凝集処理工程において凝集剤の自動注入を行うものである(請求項8の発明)。   The continuous control system of the water purification process of the present invention is based on the information on the precipitated water turbidity and filtered water turbidity obtained from any one of the water purification automatic continuous monitoring devices of 1 to 6 above, and the cause of the water purification treatment failure is minute. It is determined whether or not the filtration trouble is caused by plankton, and when it is judged that the filtration trouble is caused by microplankton, the flocculant is automatically injected in the coagulation treatment step after the implementation (the invention of claim 8).

本発明によれば、浄水処理自動連続式監視装置におけるフロック形成からろ過までの水処理に相当する滞留時間を1時間以内の短時間とすることで、実施設での凝集剤使用の合理化、適正化が可能となるとともに、凝集不全等の予防検知が可能となるので、浄水プロセスにおける危機管理能力が飛躍的に向上する。   According to the present invention, the retention time corresponding to the water treatment from floc formation to filtration in the water purification automatic continuous monitoring device is set to a short time of 1 hour or less, thereby rationalizing the use of the flocculant in the implementation facility, proper The risk management capability in the water purification process is dramatically improved.

図1は一般的な浄水場における浄水プロセスを示すものであり、本発明の浄水処理自動連続式監視装置が、実施設の浄水場における水処理薬品注入工程および混和池における攪拌工程が終了した前処理水の一部を導水する装置であることを示すものである。FIG. 1 shows a water purification process in a general water purification plant. Before the water treatment chemical injection step in the water purification plant of the present invention and the stirring step in the mixing pond are completed by the water purification treatment automatic continuous monitoring device of the present invention. It shows that it is a device for guiding a part of treated water. 図2は本発明の浄水処理自動連続式監視装置の各ユニットを示すものである。FIG. 2 shows each unit of the water purifying automatic continuous monitoring apparatus of the present invention. 図3は傾斜板沈降装置付薬品沈殿池ユニットにおける傾斜板沈降装置を示すものである。FIG. 3 shows an inclined plate settling device in a chemical sedimentation basin unit with an inclined plate settling device. 図4は傾斜板沈降装置付薬品沈殿池ユニットを示すものである。FIG. 4 shows a chemical sedimentation basin unit with an inclined plate sedimentation device. 図5は越流槽における迂流壁の作用を示す模式図である。FIG. 5 is a schematic diagram showing the action of the bypass wall in the overflow tank. 図6は浄水プロセスの連続式監視装置の導水位置を示すものである。FIG. 6 shows the water introduction position of the continuous monitoring device for the water purification process. 図7は浄水プロセスの連続式監視装置のフローチャートを示すものである。FIG. 7 shows a flowchart of the continuous monitoring device for the water purification process. 図8は浄水プロセスの連続制御システムのフローチャートを示すものである。FIG. 8 shows a flowchart of the continuous control system of the water purification process. 図9は装置の滞留時間を計測したものであるFig. 9 shows the measured residence time of the device. 図10は浄水処理自動連続式監視装置の沈殿水濁度の計測結果を示すものである。FIG. 10 shows the measurement result of the sediment water turbidity of the water purification automatic continuous monitoring system. 図11は浄水処理自動連続式監視装置のろ過水濁度の計測結果を示すものである。FIG. 11 shows the measurement results of the filtered water turbidity of the water purification process automatic continuous monitoring device. 図12は実施設のろ過水粒子数と原水ピコプランクトン数の変化を示すものである。FIG. 12 shows changes in the number of filtered water particles and the number of raw water picoplankton in the implementation facility.

以下に、添付図面を参照しながら、本発明に係る浄水処理自動連続式監視装置及びそれを用いた浄水プロセスの連続式監視システムについて、その実施の形態について説明する。
本発明は、浄水処理自動連続式監視装置におけるフロック形成からろ過までの水処理に相当する滞留時間を1時間以内の短時間とすることを目標とし、特に急速ろ過池としての処理性能を損なうことなく、滞留時間を短くすることを可能とした浄水処理自動連続式監視装置である。
なお、処理機能を損なうことなくとは、急速ろ過池ユニットで処理した後の平時におけるろ過水濁度が実施設と同等である0.05度を目標とすることである。
DESCRIPTION OF EMBODIMENTS Hereinafter, embodiments of a water purification process automatic continuous monitoring apparatus and a water purification process continuous monitoring system using the same will be described with reference to the accompanying drawings.
The present invention aims to reduce the residence time corresponding to water treatment from floc formation to filtration in a water purification automatic continuous monitoring system to a short time within 1 hour, particularly impairing the treatment performance as a rapid filtration basin. In addition, it is a water purification automatic continuous monitoring device that makes it possible to shorten the residence time.
In addition, without impairing a processing function, it is aiming at 0.05 degree | times whose filtration water turbidity in the normal time after processing with a rapid filtration basin unit is equivalent to an implementation facility.

浄水場における一般的な水処理プロセスは、図1に示すとおり、河川や貯水池などの水源から原水が着水井に取り込まれ、混和池において水処理薬品としてpH調整剤、酸化剤、および凝集剤が注入され、急速攪拌機等で攪拌および混合された後、フロック形成池、薬品沈殿池、急速ろ過池を経て浄水池に送られる。
本発明の浄水プロセスの連続制御システムは、上記の実施設の浄水設備において、水処理薬品注入工程および攪拌工程が終了した前処理水の一部を本発明の浄水処理自動連続式監視装置に導き、該監視装置の濁度監視ユニットからの情報をもとに実施設における原水の薬注制御を行なうものである。
As shown in Fig. 1, the general water treatment process at a water treatment plant is that raw water is taken into a landing well from a water source such as a river or a reservoir, and a pH adjusting agent, an oxidizing agent, and a flocculant are used as water treatment chemicals in the mixing pond. After being injected, stirred and mixed with a rapid stirrer, etc., it is sent to a clean water basin through a flock formation pond, a chemical sedimentation pond, and a rapid filtration pond.
The continuous control system of the water purification process of the present invention leads to a part of the pretreated water after the water treatment chemical injection step and the stirring step are completed in the water purification facility of the above implementation to the water purification automatic continuous monitoring device of the present invention. Based on the information from the turbidity monitoring unit of the monitoring device, the raw water chemical injection control in the implementation facility is performed.

そして、本発明の浄水処理自動連続式監視装置は、図2に示すとおり、従来の監視装置とは異なり、ろ過後の水質を測定するものである点に特徴を有するものであり、実際の急速ろ過池で処理された後のろ過水濁度に対応した監視を可能としたものである。
本発明で新たに開発された急速ろ過池ユニットで使用するろ過カラムは、急速ろ過池ユニットにおける滞留時間の短縮等を図るために幾つかの改良が施されており、以下にその改良点について説明する。
And, as shown in FIG. 2, the water purifying automatic continuous monitoring device of the present invention is characterized in that it measures the quality of water after filtration, unlike the conventional monitoring device. It enables monitoring corresponding to the filtrate turbidity after being treated in the filter basin.
The filtration column used in the rapid filtration pond unit newly developed in the present invention has been improved several times in order to shorten the residence time in the rapid filtration pond unit, and the improvements are described below. To do.

まず、ろ過カラムへの導水は、装置規模を考慮してカスケード方式を採用するものであるが、その場合、未ろ水が水面に落下する際に砂層表面をかく乱し、ろ過性能を左右する不陸を形成する問題があった。
そこで、本発明では、図2の13に示すとおり、ろ過カラムの水落下面に不陸防止用阻流装置を設けることにより、その不陸の問題点の改善を図っていることも特徴の一つである。
First, the water introduction to the filtration column adopts a cascade method in consideration of the scale of the device, but in that case, when unfiltered water falls on the water surface, the sand layer surface is disturbed, and the filtration performance is affected. There was a problem forming the land.
Therefore, in the present invention, as shown in 13 of FIG. 2, it is one of the features that the problem of the unevenness is improved by providing an obstruction prevention device on the water falling surface of the filtration column. It is.

また、急速ろ過池ユニットは、運転とともに目詰まりするために定期的な洗浄が必要であり、そのためにろ過カラムの底部に固定支持板を設け逆洗処理を容易に行なえるようにし、時間設定又は水位計の水位設定に基づく自動洗浄機能が設けられている。
さらに、洗浄時には監視装置としての機能が停止するので、定期的な洗浄間隔をできるだけ長くする必要があり、この定期洗浄間隔の延伸化も従来からの課題であった。
In addition, the rapid filtration basin unit needs to be periodically cleaned to become clogged with operation.For this purpose, a fixed support plate is provided at the bottom of the filtration column so that the backwash process can be easily performed, and time setting or An automatic cleaning function based on the water level setting of the water level gauge is provided.
Furthermore, since the function as a monitoring device stops at the time of cleaning, it is necessary to make the periodic cleaning interval as long as possible, and extending the periodic cleaning interval has also been a conventional problem.

このため、急速ろ過池ユニットに導入される沈殿水の微細な固形物の除去を図るために、本発明では急速ろ過池ユニットの前段に設置されるフロック形成池ユニット及び傾斜板沈降装置付き薬品沈殿池ユニットに対しても幾つかの改良を図るものである。
通常、薬品沈殿池では、沈殿効率を確保するために傾斜板沈降装置が設置されている。この沈降装置の仕様は、原水の水質や凝集剤注入率に依存するが、従来の装置では一定仕様の沈降装置が設置されているのみであり、原水条件などに即応した仕様とはなっていなかった。
For this reason, in order to remove the fine solid matter of the precipitated water introduced into the rapid filtration basin unit, in the present invention, a chemical precipitation with a floc formation pond unit and an inclined plate settling device installed in the preceding stage of the rapid filtration basin unit is performed. Some improvements will be made to the pond unit.
Usually, in a chemical sedimentation basin, an inclined plate sedimentation device is installed to ensure sedimentation efficiency. The specifications of this settling device depend on the quality of raw water and the injection rate of the coagulant, but the conventional device only has a settling device with a fixed specification, and it is not a specification that responds immediately to the conditions of the raw water. It was.

特に、ろ過水濁度0.05度を目標とした監視装置では、傾斜板沈降装置付き薬品沈殿池ユニットの目標濁度を1.0未満に設定する必要があるが、このためには傾斜板沈降装置の仕様を改良することが必要であった。このため、本発明の傾斜板沈降装置付き薬品沈殿池ユニットでは、原水の水質や凝集剤注入率に応じて、図3に示す傾斜板ピッチの異なる傾斜板沈降装置を取替え可能な構造とするものである。
また、従来の薬品沈殿地では、汚泥排出量、排出間隔が原水水質、水処理条件によって変化する。汚泥排出時は監視装置としての機能が停止するので、汚泥排出間隔の延伸化が課題であるとともに、排泥後の再起動時には処理が不安定となり、濁質分がろ過池に流出し、監視装置としての機能を損なう要因ともなるので、新たな装置としては改良すべき課題があった。
In particular, in a monitoring device that targets a filtered water turbidity of 0.05 degrees, it is necessary to set the target turbidity of a chemical sedimentation basin unit with an inclined plate settling device to less than 1.0. It was necessary to improve the specifications of the settling device. For this reason, in the chemical sedimentation basin unit with an inclined plate settling device of the present invention, the inclined plate settling device with different inclined plate pitches shown in FIG. 3 can be replaced according to the quality of raw water and the coagulant injection rate. It is.
Moreover, in the conventional chemical sedimentation site, sludge discharge amount and discharge interval vary depending on raw water quality and water treatment conditions. Since the function as a monitoring device stops when sludge is discharged, the extension of the sludge discharge interval is an issue, and when restarting after the sludge is discharged, the treatment becomes unstable and the turbid matter flows out to the filtration pond. Since it also becomes a factor which impairs the function as a device, there is a problem to be improved as a new device.

上記の課題に対処するため、本発明の傾斜板沈降装置付き薬品沈殿池ユニットでは、沈殿槽に図4に示す汚泥流出防止用阻流装置を設置し、濁質分がろ過ユニットに流出することを防ぐと共に、越流槽の迂流壁の上部を図5に示すような滑らかな傾斜構造とすることにより、沈殿除去し得なかった微細フロックが流出した場合もそのフロックがさらに細かく破壊分散しないように設計されている。   In order to cope with the above problem, in the chemical sedimentation basin unit with an inclined plate sedimentation device of the present invention, the sludge flow prevention device shown in FIG. 4 is installed in the sedimentation tank, and the turbid matter flows out to the filtration unit. In addition, the upper part of the bypass wall of the overflow tank has a smooth inclined structure as shown in FIG. 5, so that even if fine flocs that could not be removed by sediment flow out, the flocs will not break down and disperse more finely. Designed to be

フロック形成池ユニットにおいても、複数の攪拌機が原水水質に応じて互いに独立して回転速度の調整が可能な構成とすることによりフロック形成を効果的に行い、ろ過装置への負荷を減らすことが可能な構造となっている。
濁度監視ユニットは、沈殿水とろ過水の両方の処理水を監視するものであり、監視手段としては濁度計単独でもよいが、濁度計と微粒子カウンターを併用することによって、より正確な監視が可能である。
Even in the floc formation pond unit, it is possible to effectively form flocs and reduce the load on the filtration device by adopting a configuration in which multiple agitators can adjust the rotation speed independently of each other according to the raw water quality It has a simple structure.
The turbidity monitoring unit monitors the treated water of both precipitated water and filtered water, and the turbidimeter alone may be used as a monitoring means, but more accurate by using a turbidimeter and fine particle counter together. Monitoring is possible.

そして、本発明の浄水処理自動連続式監視装置は、フロック形成池ユニット、傾斜板沈降装置付き薬品沈殿池ユニット及び急速ろ過池ユニットが、目視観察可能な透明材料で形成されており、フロックの形成状況、沈降状況などの処理状況を目視で確認でき、さらに外部見学者に対しても本発明の浄水処理自動連続式監視装置の運転状況を分かりやすく説明することができる。   The water purification treatment automatic continuous monitoring device of the present invention includes a floc formation basin unit, a chemical sedimentation basin unit with an inclined plate sedimentation device, and a rapid filtration basin unit, which are formed of a transparent material that can be visually observed. The processing status such as the status and the sedimentation status can be visually confirmed, and the operating status of the water purification automatic continuous monitoring device of the present invention can be explained to an outside visitor in an easy-to-understand manner.

実際の浄水場では時々刻々変化する原水水質に対応した形で原水に凝集剤、塩素剤、粉末活性を注入し、水処理に万全を期している。しかしながら、特に降雨時、原水水質が急激に変化した場合など、凝集剤などの注入制御が間に合わず水処理事故を引き起こす場合がある。また、平常時においても凝集剤注入機などの不具合による不測の水処理事故を招くこともある。   In actual water treatment plants, coagulant, chlorinating agent, and powder activity are injected into the raw water in a form corresponding to the raw water quality that changes from time to time, so that the water treatment is thorough. However, especially when it is raining, when the raw water quality changes abruptly, injection control with a flocculant or the like may not be in time, and a water treatment accident may occur. Moreover, even in normal times, an unexpected water treatment accident may be caused due to a problem such as a flocculant injection machine.

本発明の浄水プロセスの連続監視装置では、上記の浄水処理自動連続式監視装置の前段階に凝集剤、塩素剤、粉末活性炭を含む薬品注入設備ユニット、急速攪拌機を装備した混和池ユニット及び濁度計、残留塩素計を含む水質計器を具備する水質監視ユニットを設けることにより、原水水質の急変に対する水処理薬剤の適正注入率を実施設の水処理にフィードフォワードして水処理事故の未然防止を可能とするものである。また、本監視装置は全浄水プロセス所要時間を実施設の1/6から1/12に短縮していることから、実施設での凝集剤注入機などの不具合発生の事前察知が可能であり、水処理事故の拡大や未然防止を可能とするものである。   In the continuous monitoring device of the water purification process of the present invention, a chemical injection equipment unit containing a flocculant, a chlorinating agent and powdered activated carbon, a mixing pond unit equipped with a rapid stirrer, and turbidity in the previous stage of the water purification automatic continuous monitoring device By installing a water quality monitoring unit equipped with a water quality meter including a total chlorine meter and a residual chlorine meter, an appropriate injection rate of water treatment chemicals for sudden changes in raw water quality can be fed forward to the water treatment facility to prevent water treatment accidents. It is possible. In addition, since this monitoring device shortens the total water purification process time from 1/6 to 1/12 of the implementation facility, it is possible to detect in advance the occurrence of defects such as the flocculant injector at the implementation facility, It is possible to expand and prevent water treatment accidents.

現在、各地の浄水場ではろ過水への微小プランクトンの漏出に悩まされている。微小プランクトンによる濁度障害の特徴は、沈殿水濁度は通常時と変わらない状況下でろ過水濁度のみが上昇(0.1度以上)することである。この原因は微小プランクトンの濁度への寄与率がろ過水で高くなるためである。ろ過水濁度の0.1度以下管理はクリプトスポリジウム対策上、現在の水道水処理管理の最重要事項である。
本発明の浄水処理プロセスの連続監視システムは、全浄水プロセス所要時間を実施設の1/6から1/12程度に短縮して沈殿水とろ過水の濁度を監視できるので、微小プランクトン特有の濁度変化を実施設で濁度障害が発生する前に検出できる。微小プランクトンは急速ろ過池前段での凝集剤(後凝集剤)により除去可能であるので、検出した濁度異常に対する後凝集剤の注入強化を自動制御化することで、本発明の浄水処理プロセスの連続監視システムは実施設でのろ過水濁度上昇を未然に防止することができる。
Currently, water treatment plants in various regions are suffering from the leakage of microplankton into filtered water. The characteristic of turbidity disturbance caused by microplankton is that only the turbidity of filtered water increases (0.1 degree or more) under the same conditions as in normal times. This is because the contribution rate of microplankton to turbidity increases with filtered water. Control of filtered water turbidity of 0.1 degree or less is the most important current tap water treatment management as a countermeasure against Cryptosporidium.
The continuous water purification process monitoring system of the present invention can reduce the total water purification process time from 1/6 to 1/12 of the facility and monitor the turbidity of precipitated water and filtered water. Change in turbidity can be detected before turbidity failure occurs at the facility. Since microplankton can be removed by a flocculant (post-flocculant) at the front stage of the rapid filtration basin, automatic control of the post-flocculant injection enhancement for the detected turbidity abnormality is automatically controlled. The continuous monitoring system can prevent an increase in the turbidity of filtered water at the implementation facility.

以上のとおり、本発明は、フロック形成池ユニット、傾斜板沈降装置付き薬品沈殿池ユニット並びに沈殿水及びろ過水の濁度監視ユニットの改良と機能を損なうことのない急速ろ過池ユニットの新規開発により、フロック形成からろ過までの処理工程に相当する全滞留時間を1時間以内とした浄水処理自動連続式監視装置及び該浄水処理自動連続式監視装
置にその前段階の各処理工程に相当するユニットを付加した浄水プロセスの連続式監視装置に関するものであり、さらに、上記浄水処理自動連続式監視装置を用いた浄水プロセスの連続制御システムに関するものである。
As described above, the present invention is based on the new development of a floc formation pond unit, a chemical sedimentation basin unit with an inclined plate sedimentation device, and a rapid filtration pond unit that does not impair the function of sedimentation and filtered water turbidity monitoring units. The water treatment automatic continuous monitoring device with a total residence time corresponding to the treatment process from flock formation to filtration within 1 hour and the water treatment automatic continuous monitoring device are provided with units corresponding to the previous treatment steps. The present invention relates to a continuous monitoring device for the added water purification process, and further relates to a continuous control system for the water purification process using the water purification automatic continuous monitoring device.

大きさ・・幅1,450mm×奥行900mm×高さ1,300mm
材質・・・フレーム;SS400、水槽部;透明PVC
処理結果の具体例を以下に示す。
図9は浄水処理自動連続式監視装置に塩化カリウムを添加して装置の滞留時間を見たものである。装置の処理水量から計算できる装置の全滞留時間(ろ過水濁度計まで)は、約30分であるが、図9に示すようにろ過水の塩化カリウムのピーク出現時間は約30分であり、装置は所定の性能を持つことが立証できた。
Size, width 1,450mm x depth 900mm x height 1,300mm
Material: Frame; SS400, water tank; Transparent PVC
Specific examples of processing results are shown below.
FIG. 9 shows the residence time of the apparatus after adding potassium chloride to the water purification automatic continuous monitoring apparatus. The total residence time of the device (up to the filtrate turbidimeter) that can be calculated from the amount of treated water in the device is about 30 minutes, but the peak appearance time of potassium chloride in filtered water is about 30 minutes as shown in FIG. The device has been proved to have the prescribed performance.

図10は大型藻類が発生している時期の浄水処理自動連続式監視装置による監視結果である。沈殿水濁度は目標値である1度以上を示し大きく変動しているが、この原因は大型藻類によるものである。図11に示す同時期のろ過水濁度も0.1度を大幅に超過している。
しかし、7月16日を境に沈殿水とろ過水の濁度はともに低下し、それぞれ目標値である1度未満、0.05度未満を示した。この低下の原因は、実施設で凝集強化等が行われたためである。本発明の監視装置が実施設の水処理状況を適格に再現できることを示すものである。
FIG. 10 shows a monitoring result by the water purification automatic continuous monitoring apparatus when macroalgae are occurring. Precipitation water turbidity shows a target value of 1 degree or more and varies greatly, but this is due to macroalgae. The filtered water turbidity in the same period shown in FIG. 11 also greatly exceeds 0.1 degree.
However, the turbidity of the precipitated water and the filtrated water both decreased from July 16 and showed target values of less than 1 degree and less than 0.05 degree, respectively. The cause of this decrease is that cohesion strengthening was performed at the implementation facility. It shows that the monitoring apparatus of the present invention can properly reproduce the water treatment status of the implementation facility.

図12は実施設のろ過水粒子数(ピコプランクトンサイズの粒子)の変化と原水ピコプランクトン数の変化を示したものである。原水ピコプランクトン数の変化に対して、ろ過水粒子数は実施設の滞留時間である約6時間遅れで変化している。
ピコプランクトンの計数には顕微鏡観察が必要で、計数結果を得るまでに長時間を要するものであるが、実施設のろ過水粒子数はピコプランクトンの代替指標として利用することができる。
したがって、本発明の監視装置の濁度変化と実施設の粒子数変化の関係を基に、本発明の浄水プロセスの連続制御システムに基づく浄水処理の早期の適正化が可能となることを示すものである。
FIG. 12 shows a change in the number of filtered water particles (particles having a picoplankton size) and a change in the number of raw water picoplanktons in the implementation facility. In contrast to the change in the number of raw water picoplankton, the number of filtered water particles changes with a delay of about 6 hours, which is the residence time of the implementation facility.
The counting of picoplankton requires microscopic observation, and it takes a long time to obtain the counting result, but the number of filtered water particles in the implementation can be used as an alternative index for picoplankton.
Therefore, based on the relationship between the change in turbidity of the monitoring device of the present invention and the change in the number of particles in the implementation facility, it indicates that it is possible to optimize the water purification process early based on the continuous control system of the water purification process of the present invention. It is.

本発明は、実施設の浄水設備を小型化した、フロック形成池ユニット、傾斜板沈降装置
付き薬品沈殿池ユニット、急速ろ過池ユニット並びに沈殿水及びろ過水の濁度監視ユニットを有する浄水処理自動連続式監視装置であり、フロック形成からろ過までの水処理所要時間を実施設の1/6から1/12程度に短縮することによって浄水処理状態を早期に監視することができ、実施設での凝集剤使用の合理化、適正化が可能となるとともに、凝集不全等の予防検知が可能となるので、浄水プロセスにおける危機管理能力が飛躍的に向上するものである。
The present invention is a water purification process automatic continuous having a floc formation pond unit, a chemical sedimentation basin unit with a sloping plate sedimentation device, a rapid filtration basin unit, and a turbidity monitoring unit for sedimentation water and filtered water. It is a type monitoring device, and the water treatment time from floc formation to filtration can be monitored at an early stage by shortening the time required for water treatment from 1/6 to 1/12 of the implementation facility. The use of chemicals can be rationalized and optimized, and preventive detection such as coagulation failure can be performed, so that the crisis management ability in the water purification process is dramatically improved.

1 フロック形成池ユニット
2 攪拌機
3 傾斜板沈降装置付き薬品沈殿池ユニット
4 傾斜板沈降装置
5 傾斜板ピッチ
6 汚泥
7 汚泥流出防止用阻流装置
8 自動排泥装置
9 越流槽
10 迂流壁
11 急速ろ過池ユニット
12 濁度監視ユニット
13 不陸防止用阻流装置
14 ろ過砂
15 固定支持板
16 水位計
1 Flock formation pond unit 2 Stirrer
3 Chemical sedimentation basin unit with inclined plate settling device 4 Tilted plate settling device 5 Tilted plate pitch 6 Sludge 7 Sludge prevention device for sludge outflow prevention 8 Automatic drainage device
DESCRIPTION OF SYMBOLS 9 Overflow tank 10 Detour wall 11 Rapid filtration pond unit 12 Turbidity monitoring unit 13 Intrusion prevention device 14 Filter sand 15 Fixed support plate 16 Water level meter

Claims (7)

実施設の浄水設備におけるフロック形成池以降の機能を全て備え、且つ、その設備を小型化した、フロック形成池ユニット、傾斜板沈降装置付き薬品沈殿池ユニット、急速ろ過池ユニット並びに沈殿水及びろ過水の濁度監視ユニットを有する浄水処理自動連続式監視装置であって、
上記傾斜板沈降装置付き薬品沈殿池ユニットが傾斜板沈降装置、沈殿槽及び迂流壁を備えた越流槽とからなり、傾斜板沈降装置部分が傾斜板ピッチの異なる傾斜板沈降装置と交換可能であり、沈殿槽がその底部に自動排泥装置を有すると共に、下部の汚泥溜りに汚泥流出防止用阻流装置を有し、越流槽の迂流壁の上部を滑らかな傾斜構造にすることにより、沈殿水の濁度を1.0度未満とする傾斜板沈降装置付き薬品沈殿池ユニットであり、
フロック形成からろ過までの水処理所要時間を実施設の1/6から1/12程度に短縮することにより浄水処理状態を早期に監視できることを特徴とする浄水処理自動連続式監視装置。
Floc formation pond unit, chemical sedimentation basin unit with sloping plate settling device, rapid filtration basin unit, sedimentation water and filtered water that have all the functions after the floc formation pond in the actual water purification equipment and that have been downsized. A water purification automatic continuous monitoring device having a turbidity monitoring unit of
The chemical sedimentation basin unit with an inclined plate settling device consists of an inclined plate settling device, a settling tank, and an overflow tank with a bypass wall, and the inclined plate settling device can be replaced with an inclined plate settling device with a different inclined plate pitch. The sedimentation tank has an automatic mud drainage device at the bottom, and a sludge preventive device for sludge outflow prevention in the lower sludge reservoir, and the upper part of the bypass wall of the overflow tank has a smooth inclined structure. Is a chemical sedimentation basin unit with an inclined plate sedimentation device that makes the turbidity of the sedimentation water less than 1.0 degree,
A water purification treatment automatic continuous monitoring apparatus characterized in that the water treatment treatment state can be monitored early by shortening the time required for water treatment from flock formation to filtration to about 1/12 to 1/12 of the implementation facility.
上記急速ろ過池ユニットが小型ろ過カラムであり、カスケード方式により導水されると共に、不陸を解消するための不陸防止用阻流装置、ろ過層を支持する固定支持板及び時間設定又は水位計の水位設定に基づく自動洗浄機能を有し、ろ過水の濁度を0.05度以下とすることを特徴とする請求項に記載の浄水処理自動連続式監視装置。 The rapid filtration basin unit is a small filtration column, which is guided by a cascade system, and has a non-land flow prevention device for eliminating unevenness, a fixed support plate that supports the filtration layer, and a time setting or water level meter. an automatic cleaning function based on the water level setting, water treatment automatic continuous monitor of claim 1, the turbidity of the filtered water, characterized in that 0.05 degrees or less. 上記フロック形成池ユニット、傾斜板沈降装置付き薬品沈殿池ユニット及び急速ろ過池ユニットが、目視観察可能な透明材料で形成されていることを特徴とする請求項1又は2に記載の浄水処理自動連続式監視装置。 The water purification treatment automatic continuous according to claim 1 or 2 , wherein the flock formation pond unit, the chemical sedimentation basin unit with an inclined plate sedimentation device, and the rapid filtration basin unit are formed of a transparent material that can be visually observed. Type monitoring device. 上記フロック形成池ユニットが複数の攪拌機を有し、それらの攪拌機は原水水質に応じて互いに独立して回転速度の調整が可能であることを特徴とする請求項1〜のいずれかに記載の浄水処理自動連続式監視装置。 The said floc formation pond unit has a some agitator, and those agitators can adjust a rotation speed mutually independently according to raw | natural water quality, The one in any one of Claims 1-3 characterized by the above-mentioned. Clean water treatment automatic continuous monitoring device. 上記濁度監視ユニットが、濁度計又は濁度計及び微粒子カウンターを備えることを特徴とする請求項1〜のいずれかに記載の浄水処理自動連続式監視装置。 The said turbidity monitoring unit is equipped with a turbidimeter or a turbidimeter, and a fine particle counter, The water purifying automatic continuous monitoring apparatus in any one of Claims 1-4 characterized by the above-mentioned. 請求項1〜のいずれかの浄水処理自動連続式監視装置と、凝集剤、塩素剤、粉末活性
炭を含む薬品注入設備ユニットと、急速攪拌機を装備した混和池ユニットと、濁度計、残留塩素計を含む水質計器を具備する水質監視ユニットとを有し、実施設の浄水設備の機能をすべて備え、且つ、その設備を小型化し、原水の取水からろ過までの全浄水プロセス所要時間を実施設の1/6から1/12程度に短縮することにより浄水処理状態を早期に監視できることを特徴とする浄水プロセスの連続式監視装置。
And one of water treatment automatic continuous monitoring system according to claim 1-5, flocculants, pesticides, and chemical injection equipment unit containing powdered activated carbon, a mixing basin unit equipped with a rapid stirrer, a turbidimeter, residual chlorine The water quality monitoring unit has a water quality meter including a meter, has all the functions of the water purification facility on the facility, and has reduced the size of the facility to carry out the total water purification process time required from the intake of raw water to filtration. A continuous monitoring device for a water purification process, characterized in that the state of the water purification treatment can be monitored at an early stage by shortening from 1/6 to 1/12.
請求項1〜のいずれかの浄水処理自動連続式監視装置から得られた沈殿水濁度及びろ過水濁度の情報に基づき、浄水処理不良原因が微小プランクトンによるろ過障害か否かを判断し、微小プランクトンによるろ過障害と判断された時に、実施設の後凝集処理工程において凝集剤の自動注入を行うことを特徴とする浄水プロセスの連続制御システム。 Based on the information on the precipitated water turbidity and filtered water turbidity obtained from the water purification automatic continuous monitoring device according to any one of claims 1 to 5 , it is determined whether or not the cause of the water purification treatment failure is a filtration failure due to microplankton. A continuous control system for a water purification process that automatically injects a coagulant in a post-coagulation treatment step after the implementation when it is determined that the filtration trouble is caused by microplankton.
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