JP2010172872A - Muddy water treatment apparatus - Google Patents

Muddy water treatment apparatus Download PDF

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JP2010172872A
JP2010172872A JP2009021416A JP2009021416A JP2010172872A JP 2010172872 A JP2010172872 A JP 2010172872A JP 2009021416 A JP2009021416 A JP 2009021416A JP 2009021416 A JP2009021416 A JP 2009021416A JP 2010172872 A JP2010172872 A JP 2010172872A
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water
muddy water
treatment tank
tank
perforated plate
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JP4997257B2 (en
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Akihiko Okada
明彦 岡田
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OKADA SANGYO KK
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a small muddy water treatment apparatus of high performance that quickly removes suspended solids. <P>SOLUTION: A perforated plate 10 with a plurality of water passage holes 9 is installed horizontally or tilted toward the side in a treatment vessel designed so that muddy water flows upward. An upward cylindrical rising edge 11 is attached to the edge of each water passage hole 9. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、濁水内の懸濁物質を除去する濁水処理装置に関する。   The present invention relates to a muddy water treatment apparatus for removing suspended substances in muddy water.

渓流水や谷水を原水とする小規模の浄水装置として、上向性ろ過池が設置されている地域においては、夏期の雷雨や集中豪雨、台風等の異常降雨により、急激な増水で、上水道原水濁度(濁度の定義はJIS K0101による)の急上昇が頻繁に発生し、これによって、ろ過池のろ層が閉塞するという問題が発生する。
この濁水の主要な成分は、無機性物質であり、山土や砂が大半を占めている。
このような河川の上流域における濁水の流入継続時間は、中、下流域と異なり、長くとも数時間ということが多い。
In areas where upward filter ponds are installed as small-scale water purification devices that use mountain stream water and valley water as raw water, the water supply will be drastically increased due to abnormal rainfall such as thunderstorms, torrential rains and typhoons in summer Sudden increase in turbidity (turbidity is defined by JIS K0101) frequently occurs, which causes a problem that the filter bed of the filter basin is clogged.
The main component of this muddy water is an inorganic substance, and most of it is mountain soil and sand.
The inflow duration of muddy water in the upstream area of such a river is often several hours at most, unlike the middle and downstream areas.

このような問題を解決するには、濁水中の懸濁物質を除去するか、濁水の流入を阻止する以外に方法はない。
懸濁物質の除去手段としては、沈殿槽(例えば特許文献1参照)や沈殿池(例えば非特許文献1参照)が知られている。
非特許文献1には、緩速ろ過池の流入原水の濁度は、概ね10度以下と定められている。ただし、原水の濁度上昇に対して、沈殿処理または一次ろ過設備を、緩速ろ過の前に追加して対応できるとしている。なお、普通沈殿池や沈殿槽においての滞留時間は約8時間である。
しかし、沈殿池や沈殿槽は広い面積を要し、山間部の小規模浄水施設では、地形や面積等の制約から、設置していないところが多い。
In order to solve such a problem, there is no method other than removing suspended substances in muddy water or preventing inflow of muddy water.
As means for removing suspended substances, a sedimentation tank (for example, see Patent Document 1) and a sedimentation tank (for example, see Non-Patent Document 1) are known.
Non-Patent Document 1 stipulates that the turbidity of the raw water in the slow filtration basin is approximately 10 degrees or less. However, it is said that precipitation treatment or primary filtration equipment can be added to the turbidity increase of the raw water before the slow filtration. In addition, the residence time in a normal sedimentation tank or a sedimentation tank is about 8 hours.
However, sedimentation basins and sedimentation tanks require a large area, and many small-scale water purification facilities in mountainous areas are not installed due to restrictions on topography and area.

濁水の流入を阻止する手段としては、高濁度感知システムにより、高濁度時に原水の流入を停止する等の制御を行い、ろ過池のろ層閉塞を防止するようにしたものがある。
この手段では、原水の流入が停止するため、その間は、浄水が得られない。断水を避けるためには、浄水を貯留する大きな配水池が必要となるが、高濁度が継続する時間は推定の域を出ないため、この大きさを計画することが困難となっている。また、高濁度感知システムおよび制御装置には、多額の工事費を要するとともに、管理上の難度が高いため、小規模浄水施設での採用は少ない。
As a means for preventing the inflow of turbid water, there is one that prevents the clogging of the filtration basin by performing control such as stopping the inflow of raw water at the time of high turbidity by a high turbidity sensing system.
With this means, since the inflow of raw water stops, clean water cannot be obtained during that time. In order to avoid the water outage, a large reservoir for storing the purified water is required, but the time during which high turbidity continues does not deviate from the estimated range, so it is difficult to plan this size. In addition, the high turbidity detection system and the control device require a large amount of construction cost and are difficult to manage, so that they are rarely used in small-scale water purification facilities.

特開2008−229437号公報JP 2008-229437 A

「水道施設設計指針 2000年度版」日本水道協会発行“Water Supply Facility Design Guidelines 2000” published by Japan Water Works Association

ろ過池のろ層の閉塞を回復したり、浄化機能を維持するためには、ろ層の洗浄作業が欠かせない。上向性ろ過池の標準的な洗浄頻度は、1年に1〜2回であるが、雷雨、台風、集中豪雨等の高濁度原水の流入の程度によっては、1年に数回ないし毎月1回、場合によっては、降雨の都度実施しなければならないこともある。緊急の洗浄作業に際しては、洗浄作業要員の緊急出動、および洗浄水量の確保が必要である。また、浄水を貯留する配水池の貯留量と使用水量である給水量とのバランスによるが、洗浄作業中に断水を余儀なくされる事態が発生することも予測される。   In order to recover the clogging of the filtration bed in the filtration basin and maintain the purification function, the washing work of the filtration bed is indispensable. The standard frequency of cleaning the upward filtration pond is 1-2 times a year, but depending on the inflow of high turbidity raw water such as thunderstorms, typhoons, and torrential rains, several times a year or every month Once, sometimes it may be necessary to carry out every rain. In an emergency cleaning operation, it is necessary to urgently dispatch cleaning personnel and to secure the amount of cleaning water. In addition, depending on the balance between the amount of water stored in the reservoir that stores the purified water and the amount of water used, which is the amount of water used, it is also predicted that there will be a situation where water must be cut off during the cleaning operation.

新設および既設の浄水装置に、濁水の流入態様に応じた効果的な除濁の機能を有する濁水処理装置を前置することにより、障害が回避され、不安が解消される。また、この濁水処理装置は、狭隘な場所に設置されることが多いことから、小型化できることが望ましい。   By installing a muddy water treatment apparatus having an effective turbidity function according to the inflow mode of muddy water in front of the new and existing water purification apparatus, obstacles are avoided and anxiety is eliminated. Moreover, since this muddy water treatment apparatus is often installed in a narrow place, it is desirable that it can be miniaturized.

本発明は、上記のような状況に鑑み、小型、高性能で、迅速に懸濁物質を除去できるようにした濁水処理装置を提供することを目的としている。   In view of the above situation, an object of the present invention is to provide a muddy water treatment apparatus that is small in size, high in performance, and capable of quickly removing suspended substances.

本発明によると、上記課題は、次のようにして解決される。
(1) 濁水が上方に向かって流通するようにした処理槽内に、複数の通水孔を穿設した多孔板を、水平または側方に傾斜させて配設するとともに、前記各通水孔の縁に、上向筒状の起立縁を設ける。
According to the present invention, the above problem is solved as follows.
(1) In a treatment tank in which muddy water flows upward, a perforated plate having a plurality of water passage holes is disposed so as to be inclined horizontally or laterally. An upright cylindrical standing edge is provided at the edge of the skirt.

このような構成とすると、濁水が多孔板の各通水孔を上方に向かって通過する際に、一時的に流速が大となり、その側部においては、ベルヌーイの定理に従って減圧され、通水孔の通過流を中心とする放射方向に渦流が発生し、濁水中の懸濁物質は、この渦流に乗って、多孔板の上面における通水孔の外周部に滞留する。
多孔板の上面に滞留した懸濁物質は、渦流の巻き込み作用により、通水孔に向って移動させられようとするが、通水孔の縁には、上向筒状の起立縁が設けられているので、懸濁物質は、通水孔を通過する濁水と合流することなく、多孔板の上面に滞留し続ける。
したがって、濁水が各通水孔を通過した後、懸濁物質は迅速に多孔板上に沈殿するので、懸濁物質の除去効率を高めることができるとともに、多孔板に多数の起立縁付きの通水孔を設けることにより、小型、高性能化を図ることができる。
With such a configuration, when turbid water passes upward through each water passage hole of the perforated plate, the flow velocity temporarily increases, and at the side thereof, the pressure is reduced according to Bernoulli's theorem, A vortex flow is generated in a radial direction centering on the passing flow, and suspended substances in muddy water ride on this vortex flow and stay on the outer periphery of the water passage hole on the upper surface of the perforated plate.
Suspended matter staying on the upper surface of the perforated plate tends to move toward the water passage hole due to the vortexing action, but the edge of the water passage hole is provided with an upright cylindrical standing edge. Therefore, the suspended substance continues to stay on the upper surface of the perforated plate without joining the turbid water passing through the water passage holes.
Therefore, after the turbid water passes through each water passage hole, the suspended substance quickly settles on the perforated plate, so that the removal efficiency of the suspended substance can be improved and the permeated plate has a large number of standing edges. By providing the holes, it is possible to reduce the size and improve the performance.

(2) 上記(1)項において、処理槽内に、複数の多孔板を多段状に配設する。   (2) In the above item (1), a plurality of perforated plates are arranged in a multistage manner in the treatment tank.

このような構成とすると、さらに小型、高性能化を図ることができる。   With such a configuration, further miniaturization and higher performance can be achieved.

(3) 上記(1)または(2)項において、起立縁の高さを、3〜7mmとする。   (3) In the above item (1) or (2), the height of the standing edge is 3 to 7 mm.

このような構成とすると、多孔板の上面に滞留した懸濁物質が、渦流の巻き込み作用により、通水孔に向って移動させられ、通水孔を通過する濁水と合流するのを確実に阻止することができる。
なお、多孔板の上面に滞留することが予測される懸濁物質の量に基づいて、起立縁の高さを、上記の範囲内において適宜定めるのがよい。
With such a configuration, the suspended matter staying on the upper surface of the perforated plate is moved toward the water passage hole by the vortexing action, and it is reliably prevented from joining the muddy water passing through the water passage hole. can do.
Note that the height of the rising edge may be appropriately determined within the above range based on the amount of suspended solids expected to stay on the upper surface of the porous plate.

(4) 上記(1)〜(3)項のいずれかにおいて、処理槽内に、多孔板を側方に傾斜させて設けるとともに、多孔板の下端側に、沈殿物を沈殿物滞留部に導く流下樋を設ける。   (4) In any one of the above items (1) to (3), the perforated plate is provided in the treatment tank so as to be inclined to the side, and the precipitate is led to the sediment retaining portion on the lower end side of the perforated plate. Provide a streamer.

このような構成とすると、長期間に亘って処理作業を継続することができ、多孔板上に滞留した懸濁物質の洗浄による除去作業の回数を少なくすることができる。   With such a configuration, the processing operation can be continued for a long period of time, and the number of removal operations by washing of the suspended substance retained on the perforated plate can be reduced.

(5) 上記(1)〜(4)項のいずれかにおいて、処理槽の上部に、上向流ろ過手段を配設する。   (5) In any one of the above items (1) to (4), an upward flow filtering means is disposed in the upper part of the treatment tank.

このような構成とすると、本発明の濁水処理装置を、上向流ろ過装置に、その前処理手段として、一体的に組み込むことができ、設置スペースの削減、設置費用の低減、および処理効率の向上を図ることができる。   With such a configuration, the turbid water treatment device of the present invention can be integrated into the upward flow filtration device as its pretreatment means, reducing installation space, reducing installation costs, and treating efficiency. Improvements can be made.

(6) 上記(1)〜(5)項のいずれかにおいて、処理槽の下端部に、ドレン管を接続し、かつ処理槽内における多孔板の上方に、多孔板上に滞留した沈殿物を洗浄する洗浄装置を設ける。   (6) In any one of the above items (1) to (5), a drain pipe is connected to the lower end portion of the treatment tank, and the precipitate retained on the porous plate is located above the porous plate in the treatment tank. A cleaning device for cleaning is provided.

このような構成とすると、多孔板上に滞留した懸濁物質の量が大となったとき、一旦濁水処理作業を一時的に停止して、滞留した懸濁物質を迅速に洗浄し、ドレン管より排出することができる。   With such a configuration, when the amount of suspended matter retained on the perforated plate becomes large, the turbid water treatment operation is temporarily stopped, and the retained suspended matter is quickly washed, and the drain tube It can be discharged more.

本発明によると、小型、高性能で、迅速に懸濁物質を除去できるようにした濁水処理装置を提供することができる。   According to the present invention, it is possible to provide a muddy water treatment apparatus that is small in size, high in performance, and capable of quickly removing suspended substances.

本発明の濁水処理装置の第1の実施形態の模式的縦断正面図である。It is a typical longitudinal section front view of a 1st embodiment of a muddy water treatment device of the present invention. 作用を説明するための多孔板の一部の拡大縦断正面図である。It is an enlarged vertical front view of a part of the porous plate for explaining the operation. 比較例を示す、図2と同様の拡大縦断正面図である。It is an enlarged vertical front view similar to FIG. 2, showing a comparative example. 本発明の濁水処理装置の第2の実施形態の模式的縦断正面図である。It is a typical vertical front view of 2nd Embodiment of the muddy water processing apparatus of this invention. 本発明の濁水処理装置の効果を説明するための実験装置と、それへの原水供給装置との模式的縦断正面図である。It is a typical vertical front view of the experimental apparatus for demonstrating the effect of the muddy water processing apparatus of this invention, and the raw | natural water supply apparatus to it.

以下、本発明の実施形態を、添付図面を参照して説明する。
図1は、本発明の濁水処理装置1を、原水を浄化して上水とするための浄化装置(図示略)の前処理装置として使用する場合の第1の実施形態を示す。
図1に示すように、この濁水処理装置1は、懸濁物質が流入して濁水となった原水2が上方に向かって流通するようにした処理槽3を備えている。
Hereinafter, embodiments of the present invention will be described with reference to the accompanying drawings.
FIG. 1 shows a first embodiment when a muddy water treatment apparatus 1 according to the present invention is used as a pretreatment apparatus for a purification apparatus (not shown) for purifying raw water into clean water.
As shown in FIG. 1, this muddy water treatment apparatus 1 includes a treatment tank 3 in which raw water 2 that has become suspended due to inflow of suspended substances flows upward.

処理槽3の底面3aは、中央に向かって下向傾斜するロート状としてあり、その中央部には、ドレン弁4を備えるドレン管5が設けられている。
処理槽3の下部には、原水供給源6に接続され、かつ流入弁7を備える流入管8が設けられており、この流入管8の先端は、処理槽3の下部中央において開口している。
The bottom surface 3a of the processing tank 3 has a funnel shape that is inclined downward toward the center, and a drain pipe 5 including a drain valve 4 is provided at the center.
An inflow pipe 8 connected to the raw water supply source 6 and provided with an inflow valve 7 is provided at the lower part of the treatment tank 3, and the tip of the inflow pipe 8 opens at the lower center of the treatment tank 3. .

処理槽3内には、図2に示すように、複数の通水孔9が、予め定めたパターンで穿設された複数の多孔板10が、それぞれ水平をなして、上下多段状に配設されている。   In the treatment tank 3, as shown in FIG. 2, a plurality of perforated plates 10 each having a plurality of water passage holes 9 formed in a predetermined pattern are horizontally arranged in upper and lower stages. Has been.

図2に示すように、各多孔板10における各通水孔9の縁には、上向筒状の起立縁11が設けられている。
多孔板10の材質は、特に限定する必要はなく、金属または合成樹脂により形成することができる。
起立縁11の高さは、3〜7mmとするのが好ましい。
As shown in FIG. 2, an upward cylindrical standing edge 11 is provided at the edge of each water passage hole 9 in each porous plate 10.
The material of the porous plate 10 is not particularly limited, and can be formed of metal or synthetic resin.
The height of the standing edge 11 is preferably 3 to 7 mm.

各段の多孔板10の通水孔9の孔径、通水孔9の相互の間隔、起立縁11の高さ等は、例えば下段のものほど、それらを大とする等、互いに異ならせて実施してもよい。   The hole diameter of the water passage holes 9 of the perforated plate 10 in each stage, the interval between the water passage holes 9, the height of the standing edge 11, etc. are made different from each other, for example, the lower one is made larger. May be.

最上段の多孔板10より上方における処理槽3の上部側面には、処理槽3内の原水2の水位が予め定めた水位以上となったとき、濁水処理された原水2が溢流するようにした流出管12が設けられている。   On the upper side surface of the treatment tank 3 above the uppermost porous plate 10, when the water level of the raw water 2 in the treatment tank 3 is equal to or higher than a predetermined water level, the muddy water-treated raw water 2 overflows. An outflow pipe 12 is provided.

また、処理槽3の上部には、洗浄弁13を介して原水供給源6またはその他の水源に接続された、洗浄装置をなす散水管14が設けられており、この散水管14の下面には、多数の散水ノズル14aが設けられている。   Further, at the upper part of the treatment tank 3, there is provided a water spray pipe 14 that is connected to the raw water supply source 6 or other water source via a cleaning valve 13 and forms a cleaning device. A large number of watering nozzles 14a are provided.

処理槽3のいずれかの側壁3bには、必要に応じて、透明のガラス板等を液密に嵌合して形成した観察窓15を設けておくのがよい。   An observation window 15 formed by liquid-tight fitting a transparent glass plate or the like may be provided on any side wall 3b of the processing tank 3 as necessary.

原水供給源6の出口部分には、原水供給源6の原水2を、流入管8および散水管14側と、バイパス管16側とに選択的に供給する第1切換弁17が設けられている。
また、バイパス管16の出口端と、流出管12の出口端とは、第2切換弁18を介して、上記浄化装置(図示略)における原水流入管19に接続され、バイパス管16を通って送られてきた原水2と、濁水処理装置1を通って濁水処理された原水2とを、選択的に原水流入管19に供給しうるようになっている。
A first switching valve 17 that selectively supplies the raw water 2 of the raw water supply source 6 to the inflow pipe 8 and the sprinkling pipe 14 side and the bypass pipe 16 side is provided at the outlet portion of the raw water supply source 6. .
The outlet end of the bypass pipe 16 and the outlet end of the outflow pipe 12 are connected to the raw water inflow pipe 19 in the purification device (not shown) via the second switching valve 18, and pass through the bypass pipe 16. The raw water 2 that has been sent and the raw water 2 that has been subjected to muddy water treatment through the muddy water treatment device 1 can be selectively supplied to the raw water inflow pipe 19.

第1および第2切換弁17、18、ドレン弁4、流入弁7、洗浄弁13等のすべての弁は、手動操作により開閉するようにしてもよいが、図1に模式的に示す制御装置20の指令によって開閉させられるようにするのが好ましい。   Although all the valves such as the first and second switching valves 17 and 18, the drain valve 4, the inflow valve 7, and the cleaning valve 13 may be opened and closed manually, the control device schematically shown in FIG. It is preferable to be opened and closed by 20 commands.

特に、第1および第2切換弁17、18は、原水供給源6の原水2の濁度が予め定めた濁度以下の場合は、制御装置20の指令により、原水2がすべてバイパス管16を通るように制御され、原水供給源6の原水2の濁度を検出する濁度検出装置(図示略)が、予め定めた濁度を検出するか、または目視により原水供給源6の原水2が濁ったことを確認して、制御装置20に濁水処理装置1の作動指令を手動入力した場合は、原水2がすべて濁水処理装置1側に供給されるように、制御装置20により、同時に切り換えられるようにするのがよい。   In particular, when the turbidity of the raw water 2 of the raw water supply source 6 is equal to or lower than a predetermined turbidity, the first and second switching valves 17 and 18 are all controlled by the control device 20 so that all of the raw water 2 passes through the bypass pipe 16. The turbidity detection device (not shown) that is controlled to pass and detects the turbidity of the raw water 2 of the raw water supply source 6 detects a predetermined turbidity, or the raw water 2 of the raw water supply source 6 is visually detected. When it is confirmed that the turbid water treatment device 1 is manually input to the control device 20 after confirming that it is cloudy, the control device 20 simultaneously switches the raw water 2 to be supplied to the turbid water treatment device 1 side. It is better to do so.

次に、濁水処理装置1の作動および取り扱いについて説明する。
制御装置20に濁水処理装置1の作動指令が入力されると、ドレン弁4および洗浄弁13を閉じ、流入弁7を開く。このときの流入弁7の開度は適宜調節できるようにしておくのが好ましい。
Next, the operation and handling of the muddy water treatment apparatus 1 will be described.
When an operation command for the muddy water treatment device 1 is input to the control device 20, the drain valve 4 and the cleaning valve 13 are closed, and the inflow valve 7 is opened. It is preferable that the opening degree of the inflow valve 7 at this time can be adjusted as appropriate.

流入弁7を開くと、原水供給源6の原水2が、流入管8を通って処理槽3内に供給され、処理槽3内の原水2の水位が漸次上昇する。
処理槽3内の原水2が、各段の多孔板10の通水孔9を上方に向かって通過する際に、図2に拡大して示すように、通水孔9を通過する原水2の流速が、周囲のものより大となり、その通過流Aの外周においては、ベルヌーイの定理に従って減圧され、通過流Aを中心とする放射方向に渦流Bが発生し、原水2中の懸濁物質Cは、この渦流Bに乗って、各多孔板10の上面における通水孔9の外周部に滞留する。
When the inflow valve 7 is opened, the raw water 2 of the raw water supply source 6 is supplied into the treatment tank 3 through the inflow pipe 8, and the water level of the raw water 2 in the treatment tank 3 gradually rises.
When the raw water 2 in the treatment tank 3 passes upward through the water passage holes 9 of the perforated plates 10 in each stage, as shown in an enlarged view in FIG. The flow velocity is greater than that of the surroundings, and at the outer periphery of the passage flow A, the pressure is reduced according to Bernoulli's theorem, and a vortex B is generated in the radial direction centering on the passage flow A. Rides on the vortex B and stays in the outer peripheral portion of the water passage hole 9 on the upper surface of each porous plate 10.

多孔板10の上面に滞留した懸濁物質Cは、渦流Bの巻き込み作用により、通水孔9に向って移動させられようとするが、通水孔9の縁には、上向筒状の起立縁11が設けられているので、懸濁物質Cは、通過流Aと合流することなく、多孔板10の上面に滞留し続ける。   The suspended substance C staying on the upper surface of the perforated plate 10 tends to be moved toward the water passage hole 9 by the entrainment action of the vortex B, but the edge of the water passage hole 9 has an upward cylindrical shape. Since the standing edge 11 is provided, the suspended substance C continues to stay on the upper surface of the porous plate 10 without joining the passing flow A.

したがって、原水2は、処理槽3内を上昇するにつれて、すなわち各多孔板10を通過する毎に、懸濁物質Cが漸次除去され、流出管12に溢流する際には、大部分の懸濁物質Cが除去され、清浄化された状態で、浄化装置の原水流入管19に供給される。   Therefore, when the raw water 2 rises in the treatment tank 3, that is, each time it passes through each porous plate 10, the suspended matter C is gradually removed, and when it overflows the outflow pipe 12, most of the suspended water C is suspended. After the turbid substance C is removed and purified, the turbid substance C is supplied to the raw water inflow pipe 19 of the purification device.

図3は、多孔板10における通水孔9の縁に、起立縁11を設けなかった場合の比較例を示す。
この場合には、多孔板10の上面に滞留した懸濁物質Cは、渦流Bの巻き込み作用により、通水孔9に向って移動させられ、通過流Aと合流し、再度巻き上げられるので、懸濁物質Cの除去効率はきわめて悪い。
FIG. 3 shows a comparative example in which the standing edge 11 is not provided at the edge of the water passage hole 9 in the perforated plate 10.
In this case, the suspended substance C staying on the upper surface of the perforated plate 10 is moved toward the water flow hole 9 by the entrainment action of the vortex B, merges with the through flow A, and is wound up again. The removal efficiency of the turbid substance C is extremely poor.

いずれかの多孔板10上に滞留した懸濁物質Cの高さが、起立縁11の高さに近づいたことを、観察窓15からの視認により確認したときは、流入弁7を閉じて、流入管8からの原水2の供給を停止し、かつドレン弁4と洗浄弁13とを開いて、ドレン管5から処理槽3内の原水2と懸濁物質Cとを排出しつつ、散水管14より散水して、各多孔板10上に滞留した懸濁物質Cを洗い流す。   When it is confirmed by visual recognition from the observation window 15 that the height of the suspended substance C staying on any of the perforated plates 10 has approached the height of the standing edge 11, the inflow valve 7 is closed, While stopping the supply of the raw water 2 from the inflow pipe 8 and opening the drain valve 4 and the cleaning valve 13, the raw water 2 and the suspended matter C in the treatment tank 3 are discharged from the drain pipe 5, and the water spray pipe 14 is sprayed to wash away suspended matter C retained on each porous plate 10.

このときの多孔板10の洗浄を容易にするため、各多孔板10の全周縁またはその一部と、処理槽3の内面との間に、起立縁のない間隙を設けておくのがよい。
また、散水管14は、処理槽3内の上部だけでなく、中間部や、各多孔板10のそれぞれの上方に設けておいてもよい。
さらに、各多孔板10を、処理槽3の内面に設けたブラケット10a上に、単に載置するだけとし、そこから簡単に取り外して、洗浄できるようにしたり、各多孔板10の一方の側端部を、処理槽3の内面に水平軸(図示略)をもって枢着し、同じく他方の側端部を支持するブラケット10aを処理槽3の内面から外すか、または移動させることによって、各多孔板10が上記水平軸から下向傾斜して、洗浄しやすくなるようにしてもよい。
In order to facilitate cleaning of the perforated plate 10 at this time, it is preferable to provide a gap without an upstanding edge between the entire peripheral edge of each perforated plate 10 or a part thereof and the inner surface of the treatment tank 3.
Further, the sprinkling pipe 14 may be provided not only at the upper part in the treatment tank 3 but also at the intermediate part or above each porous plate 10.
Further, each porous plate 10 is simply placed on a bracket 10 a provided on the inner surface of the treatment tank 3, and can be easily removed from the porous plate 10 so that it can be cleaned. Each of the perforated plates is pivoted to the inner surface of the processing tank 3 with a horizontal axis (not shown), and the bracket 10a supporting the other side end is removed from the inner surface of the processing tank 3 or moved. 10 may be inclined downward from the horizontal axis to facilitate cleaning.

多孔板10の洗浄作業終了後、ドレン弁4と洗浄弁13とを閉じ、流入弁7を開くことにより、原水2からの懸濁物質Cの除去作業を再開することができる。   After the perforated plate 10 is cleaned, the drain valve 4 and the cleaning valve 13 are closed, and the inflow valve 7 is opened, so that the suspended substance C can be removed from the raw water 2 again.

図4は、本発明の濁水処理装置の第2の実施形態の模式的縦断正面図である。
この実施形態では、処理槽3の上下方向の中間部に、多数の透水孔21を穿設した水平受板22を設け、その上に、従来の上向流ろ過装置におけるのと同様の砕石、砂利、砂等を、下方から上方に向けて順に細粒化したろ過層からなる上向流ろ過手段23を設けることにより、濁水処理装置1を、上向流ろ過装置24の前処理手段として、一体的に形成したものとしてある。
FIG. 4 is a schematic longitudinal sectional front view of the second embodiment of the muddy water treatment apparatus of the present invention.
In this embodiment, a horizontal receiving plate 22 having a large number of water permeable holes 21 is provided in the middle portion in the vertical direction of the treatment tank 3, and the crushed stone is the same as that in the conventional upward flow filtration device. By providing the upward flow filtration means 23 composed of a filtration layer in which gravel, sand and the like are sequentially refined from below to above, the muddy water treatment apparatus 1 is used as a pretreatment means for the upward flow filtration apparatus 24. It is assumed that it is integrally formed.

処理槽3内における水平受板22の下方には、流入管8の上方において、中央部から両側方に向かって下向傾斜する複数の山形の多孔板25が、上下方向に多段状に設けられ、各多孔板25の両側端部には、沈殿物を沈殿物滞留部(図示略)に導く流下樋26が設けられている。   Below the horizontal receiving plate 22 in the treatment tank 3, a plurality of mountain-shaped perforated plates 25 inclined downward from the center toward both sides above the inflow pipe 8 are provided in multiple stages in the vertical direction. At both ends of each perforated plate 25, there are provided flow-down tubs 26 for guiding the precipitate to a precipitate retention portion (not shown).

山形の各多孔板25に穿設した複数の通水孔26の縁に設けた円筒形の起立縁27の高さは、傾斜の低いところにあるものほど高くしてあり、各多孔板25上に堆積した懸濁物質C(図2参照)が、傾斜の低いところにある起立縁27を乗り越えて、通水孔26を通る通過流A(図2参照)と合流しないようにしてある。
その他の構成は、第1の実施形態と同様である。
The height of the cylindrical standing edge 27 provided at the edge of the plurality of water passage holes 26 drilled in each of the mountain-shaped perforated plates 25 is higher as it is at a lower slope. Suspended substance C (see FIG. 2) deposited on the surface of the suspended material C climbs over the rising edge 27 at a low slope so as not to join the passing flow A (see FIG. 2) passing through the water passage hole 26.
Other configurations are the same as those of the first embodiment.

第2の実施形態によると、第1の実施形態におけるのと同様の作用により、各多孔板25上に沈殿した懸濁物質Cは、各多孔板25の傾斜に沿ってゆっくりと流化した後、流下樋26に沿って沈殿物滞留部に導かれる。
したがって、長期間に亘って多孔板25の洗浄作業を行う必要がなく、洗浄作業回数を少なくすることができる。
According to the second embodiment, the suspended substance C precipitated on each porous plate 25 is slowly fluidized along the inclination of each porous plate 25 by the same action as in the first embodiment. Then, it is guided to the sediment retaining portion along the downflow basin 26.
Therefore, it is not necessary to perform the cleaning operation of the porous plate 25 over a long period of time, and the number of cleaning operations can be reduced.

図5は、本発明の濁水処理装置による除濁効果の有効性を把握するための実験装置である。
原水槽30内には、攪拌装置31とポンプ32とを設け、鹿沼土を投入して、原水2を攪拌装置31により攪拌し、ポンプ32によりくみ上げた原水2を、流量調整槽33において、流量と濁度とが下記の諸元となるように調整して、流入管8より処理槽3内に供給するようにしてある。
この実験装置の諸条件は、次の通りである。
処理槽3の大きさ :縦285mm×横285mm×高さ850mm
処理槽3内の原水2の滞留時間 :1.13リットル/分・・・1.62m3/日
処理槽3内の原水2の上向流速 :20m/日・・・0.83m/時間
多孔板10の通水孔の内径と間隔:直径7mm×間隔15mm、直径5mm×間隔15mm
多孔板10の枚数 :直径7mm×2枚、直径5mm×5枚
多孔板10の上下方向の間隔 :75mm
原水2の初期濁度 :約80度
実験継続時間 :6〜8時間
FIG. 5 is an experimental apparatus for grasping the effectiveness of the turbidity effect by the muddy water treatment apparatus of the present invention.
In the raw water tank 30, a stirring device 31 and a pump 32 are provided, and Kanuma soil is introduced, the raw water 2 is stirred by the stirring device 31, and the raw water 2 pumped up by the pump 32 is flowed in the flow rate adjusting tank 33. And the turbidity are adjusted so as to have the following specifications, and are supplied into the treatment tank 3 from the inflow pipe 8.
Various conditions of this experimental apparatus are as follows.
Size of the processing tank 3: length 285 mm × width 285 mm × height 850 mm
Residence time of raw water 2 in treatment tank 3: 1.13 liters / minute ... 1.62 m3 / day Upward flow velocity of raw water 2 in treatment tank 3: 20 m / day ... 0.83 m / hour perforated plate Inner diameter and interval of 10 water passage holes: Diameter 7 mm x interval 15 mm, diameter 5 mm x interval 15 mm
Number of perforated plates 10: diameter 7 mm × 2 and diameter 5 mm × 5 perforated plates 10 in the vertical direction: 75 mm
Initial turbidity of raw water 2: about 80 degrees Experiment duration: 6-8 hours

平常時の渓流水や谷水の平均濁度は5以下であるが、降雨時には、濁度が50前後に急激に上昇し、異常降雨時には、さらにこれを超えることが多い。従来の上向流ろ過装置における原水の最高濁度は、一般的に50度であるので、これより高い約80度の濁度で実験を実施した。   The average turbidity of mountain stream water and valley water in normal times is 5 or less, but the turbidity increases rapidly to around 50 when it rains, and often exceeds this when it rains abnormally. Since the maximum turbidity of raw water in a conventional upward flow filtration apparatus is generally 50 degrees, the experiment was conducted at a turbidity of about 80 degrees higher than this.

実験継続時間を6〜8時間としたのは、渓流水や谷水の場合、降雨初期の濁度上昇は大きいが、降雨が継続していても数時間後には、濁度が比較的低下することを考慮したものである。   The experiment duration was set to 6 to 8 hours. In the case of mountain stream water and valley water, the turbidity rise at the beginning of the rain was large, but the turbidity was relatively lowered after several hours even if the rain continued. Is taken into account.

この実験装置の除濁効果の有効性を確認するため、同一の実験装置を用いて、多孔板10をすべて取り外し、他の条件をすべて同一として、自然沈降分離のみによる空運転を実施し、濁度の変化を観察した。その結果は、表1および表2に示すとおりである。

Figure 2010172872
Figure 2010172872
In order to confirm the effectiveness of the turbidity-eliminating effect of this experimental apparatus, using the same experimental apparatus, all the perforated plates 10 were removed, all other conditions were the same, and the empty operation was carried out only by natural sedimentation separation. The degree change was observed. The results are as shown in Tables 1 and 2.
Figure 2010172872
Figure 2010172872

この実験結果から明らかなように、空運転での濁質分の除去率が5.7%であるのに対して、多孔板10を用いたものでは、濁質分の除去率は35.3%である。この差は、本発明の濁水処理装置が、大きな除濁作用を有していること示している。   As is apparent from the experimental results, the removal rate of turbid matter in the idling operation is 5.7%, whereas the removal rate of turbid matter is 35.3 when the porous plate 10 is used. %. This difference indicates that the turbid water treatment apparatus of the present invention has a large turbidity-removing action.

処理水の濁度の平均値が50.20であることから、この実験装置をほぼそのまま、従来の上向流ろ過装置の前処理装置として用いることもできる。   Since the average value of the turbidity of the treated water is 50.20, this experimental apparatus can be used almost as it is as a pretreatment apparatus of a conventional upward flow filtration apparatus.

処理槽3における中間資料採取位置から採取した中間水の濁度の測定結果から、除濁作用は、多孔板10の設置段数によって異なることがわかる。
中間資料採取位置より下方で捕捉される濁質分と、同じく上方で捕捉される濁質分とは、ある程度成分が異なることは予測されるが、採取される原水2中の濁質成分に合わせて、多孔板10の設置段数、通水孔9の内径や間隔等を定めることにより、さらに効率的な除濁効果が得られるものと推測される。
From the measurement result of the turbidity of the intermediate water collected from the intermediate data collection position in the treatment tank 3, it can be seen that the turbidity is different depending on the number of installation stages of the porous plate 10.
It is expected that the turbid content captured below the intermediate data collection position and the turbid content captured similarly above will differ to some extent, but it will match the turbid content in the raw water 2 to be collected. Thus, it is presumed that a more efficient turbidity effect can be obtained by determining the number of installation stages of the perforated plate 10, the inner diameter and the interval of the water passage holes 9, and the like.

実験を行った8時間の間、ほぼ同程度の除去率が得られていることから、実際に高濁度の濁水が継続すると予測される降雨初期の数時間において、本発明の装置を有効に利用できることが証明された。   Since almost the same removal rate was obtained during the 8 hours of the experiment, the device of the present invention was effectively used in the first few hours of the rain when it was predicted that high turbid water would actually continue. Proven to be available.

なお、実験終了後、処理槽3の底部から、排泥、排水を行った後、上方から清水を散水すると、各多孔板10上に堆積した濁質成分は、上段の通水孔9から落下する洗浄水により洗浄されて、数分で処理槽3外部に排出された。   After the experiment is completed, after draining and draining from the bottom of the treatment tank 3, when clear water is sprinkled from above, turbid components deposited on the perforated plates 10 fall from the upper water passage holes 9. It was washed with washing water to be discharged and discharged to the outside of the treatment tank 3 in a few minutes.

上記の実験に用いた処理槽3は、従来の上向流ろ過装置の面積の約1/4、高さ(槽の深さ)1/2に当たる。また、この容積で、上向流速20m/日、滞留時間1時間として、濁度80の原水2を、濁度約50度まで除濁することができる。
この処理時間は、普通沈殿池の沈殿時間8時間と比較すると、1/8である。
従って、山間部の浄水装置の前処理装置等として、狭隘なスペースにも、有効に設置することができる。
The treatment tank 3 used in the above-mentioned experiment corresponds to about 1/4 of the area of the conventional upward flow filter and 1/2 of the height (depth of the tank). Further, with this volume, the raw water 2 having a turbidity of 80 can be deturbed to a turbidity of about 50 degrees with an upward flow rate of 20 m / day and a residence time of 1 hour.
This treatment time is 1/8 compared to the sedimentation time of 8 hours in the normal sedimentation basin.
Therefore, it can be effectively installed in a narrow space as a pretreatment device for a water purification device in a mountainous area.

1 濁水処理装置
2 原水(濁水)
3 処理槽
3a底面
3b側壁
4 ドレン弁
5 ドレン管
6 原水供給源
7 流入弁
8 流入管
9 通水孔
10 多孔板
10aブラケット
11 起立縁
12 流出管
13 洗浄弁
14 散水管
14a散水ノズル(洗浄装置)
15 観察窓
16 バイパス管
17 第1切換弁
18 第2切換弁
19 (浄化装置の)原水流入管
20 制御装置
21 透水孔
22 水平受板
23 上向流ろ過手段
24 上向流ろ過装置
25 多孔板
26 通水孔
27 起立縁
30 原水槽
31 攪拌装置
32 ポンプ
33 流量調整槽
1 Muddy water treatment device 2 Raw water (turbid water)
DESCRIPTION OF SYMBOLS 3 Treatment tank 3a Bottom surface 3b Side wall 4 Drain valve 5 Drain pipe 6 Raw water supply source 7 Inflow valve 8 Inflow pipe 9 Water flow hole 10 Perforated plate 10a Bracket 11 Standing edge 12 Outflow pipe 13 Washing valve 14 Sprinkling pipe 14a Watering nozzle (cleaning device) )
15 observation window 16 bypass pipe 17 first switching valve 18 second switching valve 19 (purifier) raw water inflow pipe 20 controller 21 water permeation hole 22 horizontal receiving plate 23 upward flow filtration means 24 upward flow filtration device 25 perforated plate 26 Water flow hole 27 Standing edge 30 Raw water tank 31 Stirrer 32 Pump 33 Flow rate adjusting tank

Claims (6)

濁水が上方に向かって流通するようにした処理槽内に、複数の通水孔を穿設した多孔板を、水平または側方に傾斜させて配設するとともに、前記各通水孔の縁に、上向筒状の起立縁を設けたことを特徴とする濁水処理装置。   In a treatment tank in which muddy water circulates upward, a perforated plate having a plurality of water passage holes is horizontally or laterally inclined and disposed at the edge of each water passage hole. A muddy water treatment apparatus provided with an upward cylindrical rising edge. 処理槽内に、複数の多孔板を多段状に配設した請求項1記載の濁水処理装置。   The muddy water treatment apparatus according to claim 1, wherein a plurality of perforated plates are arranged in a multistage manner in the treatment tank. 起立縁の高さを、3〜7mmとした請求項1または2記載の濁水処理装置。   The muddy water treatment apparatus according to claim 1 or 2, wherein the height of the standing edge is 3 to 7 mm. 処理槽内に、多孔板を側方に傾斜させて設けるとともに、多孔板の下端側に、沈殿物を沈殿物滞留部に導く流下樋を設けた請求項1〜3のいずれかに記載の濁水処理装置。   The turbid water according to any one of claims 1 to 3, wherein a perforated plate is provided in the treatment tank so as to be inclined to the side, and a falling gutter is provided on the lower end side of the perforated plate to guide the precipitate to the sediment retaining portion. Processing equipment. 処理槽の上部に、上向流ろ過手段を配設した請求項1〜4のいずれかに記載の濁水処理装置。   The muddy water treatment apparatus according to any one of claims 1 to 4, wherein an upward flow filtration means is disposed at an upper portion of the treatment tank. 処理槽の下端部に、ドレン管を接続し、かつ処理槽内における多孔板の上方に、多孔板上に滞留した沈殿物を洗浄する洗浄装置を設けた請求項1〜5のいずれかに記載の濁水処理装置。   The drain apparatus is connected to the lower end part of a processing tank, and the washing | cleaning apparatus which wash | cleans the deposit which stayed on the porous board was provided above the porous board in a processing tank. Turbid water treatment equipment.
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