JP6358985B2 - Method for adjusting amount of flocculant added to raw water and raw water treatment apparatus - Google Patents

Method for adjusting amount of flocculant added to raw water and raw water treatment apparatus Download PDF

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JP6358985B2
JP6358985B2 JP2015111324A JP2015111324A JP6358985B2 JP 6358985 B2 JP6358985 B2 JP 6358985B2 JP 2015111324 A JP2015111324 A JP 2015111324A JP 2015111324 A JP2015111324 A JP 2015111324A JP 6358985 B2 JP6358985 B2 JP 6358985B2
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raw water
side wall
thickener
flocculant
settling tank
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JP2016221468A (en
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伊藤 弘志
弘志 伊藤
伊藤 恭司
恭司 伊藤
伊藤 嘉浩
伊藤  嘉浩
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Ito Corp
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本発明は、凝集剤を添加して原水中の懸濁物質とともにフロックとして凝集させて上澄水と分離するシックナーにおいて沈殿物を迅速に沈降させるために原水に添加する凝集剤の添加量を適正に加減調整する原水への凝集剤添加量調整方法及び原水処理装置に関する。   In the present invention, the flocculant is added to the raw water in order to quickly settle the precipitate in the thickener that aggregates as a floc together with suspended substances in the raw water and separates from the supernatant water. The present invention relates to a method for adjusting the amount of flocculant added to raw water to be adjusted, and a raw water treatment apparatus.

シックナー内の沈殿濃度の測定は、原水中の懸濁物質の迅速な凝集沈殿を図るため、且つ高価な凝集剤の適正投入量を決定するために必要なものである。
優れた沈殿濃度の測定は超音波によるもの(例えば、特許文献1参照)が正確であるが、高価な設備費を要するため、従来はシックナーから排出された凝集物の硬化状態、或いはシックナーへ供給する原水を掬い取って目測し、凝集剤の添加量を決定していたのである。
The measurement of the concentration of the precipitate in the thickener is necessary in order to achieve a rapid coagulation sedimentation of the suspended solids in the raw water and to determine an appropriate input amount of the expensive coagulant.
The measurement of excellent precipitation concentration is accurate by ultrasonic waves (for example, see Patent Document 1), but since expensive equipment costs are required, the agglomerate discharged from the thickener is conventionally cured or supplied to the thickener. The raw water to be collected was taken and measured to determine the amount of flocculant added.

特開2013−154262号公報JP 2013-154262 A

しかしながら、目測による不正確性、或いは機械測定の場合でも隔時間測定のため即対応できない問題点があった。
このため迅速な凝集沈殿が図れず、或いは凝集剤の過大投入となって経費が増加するのである。
そこで、本発明では、シックナーに投入する原水の現在濃度を簡単な手法にて適正に測定することで凝集剤の添加量を適正に調整できる様にした原水への凝集剤添加量調整方法及び原水処理装置を提供するものである。
However, there are problems such as inaccuracy due to visual measurement, or even in the case of mechanical measurement, it cannot be dealt with immediately because it is measured every other time.
For this reason, rapid agglomeration and precipitation cannot be achieved, or the cost increases due to excessive input of the aggregating agent.
Therefore, in the present invention, the coagulant addition amount adjustment method to the raw water and the raw water so that the addition amount of the coagulant can be appropriately adjusted by appropriately measuring the current concentration of the raw water charged into the thickener by a simple method. A processing apparatus is provided.

上記課題に鑑み、本発明に係る原水への凝集剤添加量調整方法及びこの方法を用いた原水処理装置は、上流に原水を断続供給する原水ピットを設けると共に、下流に凝集剤を添加して原水からフロックを沈降分離させるシックナーを設けた一連の配管経路中にシックナーに比し小型で内部に撹拌装置を設けた沈殿槽を設け、該沈殿槽は、その上流側の側壁下部に原水ピットの下流側の側壁下部に水平配管を介して上流側の側壁上方部位を接続すると共に、複数の阻流板を上下で食い違いに内部配置した垂直配管の下流側の側壁下部を配管接続し、沈殿槽の下流側の側壁上方にシックナーの上流側の側壁上方を配管接続し、沈殿槽の底部は傾斜配管を介してシックナーの上流側の側壁下部に連結して成り、沈殿槽内の原水の濁度を計測し、その濁度に基づき前記垂直配管上端に設けた投入口から投入される凝集剤の添加量を調整することを特徴とする。 In view of the above problems, a method for adjusting the amount of flocculant added to raw water according to the present invention and a raw water treatment apparatus using this method are provided with a raw water pit for intermittently supplying raw water upstream, and adding a flocculant downstream. A settling tank that is smaller than a thickener and has a stirring device inside is provided in a series of piping paths that are provided with a thickener that separates flocs from raw water, and the settling tank has a raw water pit below the side wall on the upstream side. Connect the upper part of the upstream side wall via the horizontal pipe to the lower part of the side wall on the downstream side, and connect the lower part of the side wall on the downstream side of the vertical pipe in which a plurality of baffle plates are arranged in a staggered manner up and down. The upper side wall of the thickener is connected to the upper side wall of the thickener, and the bottom of the sedimentation tank is connected to the lower part of the side wall on the upstream side of the thickener via an inclined pipe. Measure the And adjusting the amount of the coagulant to be introduced from the provided in the vertical pipe upper end based on the time inlet.

要するに本発明は、上流に原水を断続供給する原水ピットを設けると共に、下流に凝集剤を添加して原水からフロックを沈降分離させるシックナーを設けた一連の配管経路中にシックナーに比し小型の沈殿槽を設け、該沈殿槽は、その下流側の側壁上方にシックナーの上流側の側壁上方を配管接続したので、該沈殿槽をシックナーのスケールモデルとすることができるため、沈殿槽内をシックナー内と同一環境化と見なすことができ、これにより沈殿槽内に投入した濁度計により短時間でその濁度を計測でき、かかる濁度に基づき原水への適正な凝集剤の添加量を加減調整できる等その実用的効果甚だ大である。   In short, the present invention provides a raw water pit for intermittently supplying raw water upstream, and a thicker sediment than a thickener in a series of piping paths provided with a thickener for adding flocculant downstream to settle flocs from raw water. Since a tank is provided, and the upper side wall of the thickener is connected to the upper side wall on the downstream side of the sedimentation tank, the sedimentation tank can be used as a thickener scale model. The turbidity can be measured in a short time with a turbidimeter placed in the sedimentation tank, and the amount of the appropriate flocculant added to the raw water can be adjusted based on this turbidity. Its practical effects are great.

原水処理装置の概略断面図である。It is a schematic sectional drawing of a raw water treatment apparatus. 図1の平面図である。It is a top view of FIG.

以下本発明の実施の一形態例を図面に基づいて説明する。
図に示す原水処理装置は、上流に原水Wを断続的に供給する原水ピット1を設けると共に、下流に硫酸バンドやポリ塩化アルミニウム(PAC)等の無機凝集剤(以下、単に凝集剤と称する。)を添加して原水Wからフロックを沈降分離させるシックナー2を設けた一連の配管経路中にシックナー2に比し小型の沈殿槽3を設けている。
An embodiment of the present invention will be described below with reference to the drawings.
The raw water treatment apparatus shown in the figure is provided with a raw water pit 1 for intermittently supplying raw water W upstream, and an inorganic flocculant such as a sulfuric acid band or polyaluminum chloride (PAC) (hereinafter simply referred to as a flocculant). ) And a thickener 2 that is smaller than the thickener 2 is provided in a series of piping paths provided with the thickener 2 that settles and separates flocs from the raw water W.

シックナー2は、図中では、その一部のみ表示しているに過ぎないが、従来周知のシックナーと同様に、大容量の円筒型のタンク2aを設け、該タンク2a内には、その内部に供給された凝集剤添加の原水Wの撹拌を目的とした撹拌手段(図示せず)を設けている。   Only a part of the thickener 2 is shown in the figure, but a large-capacity cylindrical tank 2a is provided in the same manner as a conventionally known thickener. Stirring means (not shown) for the purpose of stirring the supplied raw water W added with the flocculant is provided.

原水ピット1は、原水投入口1aを上方開口した有底箱型に形成されると共に、櫓4を介した所定高さ位置(図示例ではシックナー2より上方)に設置して成り、原水ピット1の前壁(下流側の側壁)下部に原水Wを送出する様に下流側へ延設した水平配管5を接続している。   The raw water pit 1 is formed in a bottomed box shape with the raw water inlet 1a opened upward, and is installed at a predetermined height position (above the thickener 2 in the illustrated example) via the trough 4, and the raw water pit 1 A horizontal pipe 5 extending downstream is connected to the lower part of the front wall (downstream side wall) so as to send the raw water W.

水平配管5は、その先端が円筒状に形成された垂直配管6の後壁(上流側の側壁)上方部位に直交接続されている。
垂直配管6は、凝集剤の投入口6aとして上端が開口されており、水平配管5との連通部位より下方内部には、複数の半円状の阻流板7を上下に所定間隔を置いて前後食い違いに水平配置しており、各阻流板7の中心部位は、垂直配管6の軸線上に配置された支持棒8に固着され、その上下位置における水平状態が保持されている。
The horizontal pipe 5 is orthogonally connected to the upper part of the rear wall (upstream side wall) of the vertical pipe 6 whose tip is formed in a cylindrical shape.
Vertical pipe 6 has an upper end as inlet 6a of flocculants are opened, the lower interior than communicating portion between the horizontal pipe 5, at a predetermined interval a plurality of semicircular baffle 7 vertically It is horizontally arranged in a front-rear direction, and the central portion of each baffle plate 7 is fixed to a support bar 8 arranged on the axis of the vertical pipe 6 so that the horizontal state in the vertical position is maintained.

垂直配管6は、その前壁(下流側の側壁)下部が連通管9を介して沈殿槽3の後壁(上流側の側壁)下部に接続されている。
連通管9の前後には、原水Wの流量調整用のバタフライ弁10の弁箱10aが介装され、該弁箱10aの上部に長尺な筒部10bを突設し、該筒部10bには、これより長い弁棒10cを水密状にして回転自在に挿通し、該弁棒10cの回転でバタフライ弁10の開度を調整する様に成している。
The vertical pipe 6 has a lower front wall (downstream side wall) lower part connected to a lower rear wall (upstream side wall) lower part of the sedimentation tank 3 via a communication pipe 9.
Before and after the communication pipe 9, a valve box 10a of a butterfly valve 10 for adjusting the flow rate of the raw water W is interposed, and a long cylinder part 10b is projected from the upper part of the valve box 10a. The valve rod 10c longer than this is made watertight and rotatably inserted, and the opening of the butterfly valve 10 is adjusted by the rotation of the valve rod 10c.

沈殿槽3は、有底筒状に形成されると共に、櫓4より低い台座フレーム11上に設置して成り、沈殿槽3の前壁(下流側の側壁)上方にタンク2aの後壁(上流側の側壁)上方を原水供給管12を介して配管接続して沈殿槽3とタンク2aを連通している。
沈殿槽3内には、撹拌装置13を設けており、該撹拌装置13は、沈殿槽3内底に配置された撹拌翼13aと、該撹拌翼13aの回転軸13bを連結した駆動源13cとから成り、該駆動源13cは、沈殿槽3の上方開口部3aの直径方向に架設されたベースフレーム14上の中央に設置されている。
The sedimentation tank 3 is formed in a cylindrical shape with a bottom and is installed on a pedestal frame 11 that is lower than the ridge 4, and the rear wall (upstream) of the tank 2 a above the front wall (downstream side wall) of the sedimentation tank 3. The upper side wall) is connected via a raw water supply pipe 12 so that the precipitation tank 3 and the tank 2a communicate with each other.
A stirrer 13 is provided in the settling tank 3, and the stirrer 13 includes a stirring blade 13a disposed at the bottom of the settling tank 3, and a drive source 13c connected to the rotating shaft 13b of the stirrer 13a. The drive source 13c is installed at the center on the base frame 14 installed in the diameter direction of the upper opening 3a of the settling tank 3.

尚、沈殿槽3の底部は、タンク2a内の後壁下部に傾斜配管15を介して連結し、該傾斜配管15は沈殿槽3底部に沈降したフロックをタンク2a内底部へ排出する様に成している。
又、垂直配管6の底部と傾斜配管15の基端とを細管16で接続し、垂直配管6底部に沈降した微砂を細管16及び傾斜配管15を介してタンク2a内底部へ排出する様に成している。
The bottom of the sedimentation tank 3 is connected to the bottom of the rear wall of the tank 2a via an inclined pipe 15. The inclined pipe 15 is configured to discharge the floc that has settled at the bottom of the precipitation tank 3 to the bottom of the tank 2a. doing.
Further, the bottom of the vertical pipe 6 and the base end of the inclined pipe 15 are connected by a thin pipe 16 so that fine sand settled on the bottom of the vertical pipe 6 is discharged to the bottom of the tank 2a through the thin pipe 16 and the inclined pipe 15. It is made.

そして、沈殿槽3内には周知の濁度計17を備え、該濁度計17により沈殿槽3内の濁度を計測する。   A well-known turbidimeter 17 is provided in the precipitation tank 3, and the turbidity in the precipitation tank 3 is measured by the turbidimeter 17.

上記構成の原水処理装置にあっては、原水ピット1から供給される原水Wは、水平配管5を経て垂直配管6へと移送される。
垂直配管6では、上下で食い違い配置された阻流板7によって原水Wを数回蛇行させ、垂直配管6上方の投入口6aから投入される凝集剤を混合させる。
In the raw water treatment apparatus having the above configuration, the raw water W supplied from the raw water pit 1 is transferred to the vertical pipe 6 through the horizontal pipe 5.
In the vertical pipe 6, the raw water W is meandered several times by the baffle plates 7 arranged in a staggered manner on the upper and lower sides, and the flocculant charged from the inlet 6 a above the vertical pipe 6 is mixed.

そして、垂直配管6を経て沈殿槽3及びシックナー2内に凝集剤が混合された原水Wが貯留される。
シックナー2では図示しない撹拌手段により、沈殿槽3では撹拌装置13により、原水Wを撹拌し、フロックを形成する。
And the raw | natural water W in which the coagulant | flocculant was mixed in the sedimentation tank 3 and the thickener 2 is stored through the vertical piping 6. FIG.
In the thickener 2, the raw water W is stirred by a stirring means (not shown) and in the sedimentation tank 3 by a stirring device 13 to form a flock.

沈殿槽3とシックナー2とは原水供給管12を介して連通しており、原水Wの供給のない静止状態では、沈殿槽3とシックナー2の水位は同じであり、沈殿槽3をシックナー2のスケールモデルとして、沈殿槽3内をシックナー2内と同一環境化と見なすことができ、これにより沈殿槽3内に投入した濁度計17により短時間でその濁度を計測でき、かかる濁度に基づき原水Wへの凝集剤添加の有無の判断や凝集剤添加量の増減を設定し、適正量の凝集剤を垂直配管6の投入口6aから添加し、沈殿槽3とシックナー2内の原水Wから生成されるフロックの沈殿分離を効率よく、その沈降分離状態を常に良好と成すことができる。   The settling tank 3 and the thickener 2 communicate with each other via the raw water supply pipe 12, and the water level of the settling tank 3 and the thickener 2 is the same when the raw water W is not supplied. As a scale model, the inside of the sedimentation tank 3 can be regarded as the same environment as the inside of the thickener 2, so that the turbidity can be measured in a short time by the turbidimeter 17 introduced into the sedimentation tank 3. Based on the determination of whether or not the flocculant is added to the raw water W and the increase / decrease in the amount of flocculant added, an appropriate amount of flocculant is added from the inlet 6a of the vertical pipe 6, and the raw water W in the sedimentation tank 3 and thickener 2 is added. The flocs produced from the precipitate can be separated efficiently, and the sedimentation state of the floc can always be made good.

1 原水ピット
2 シックナー
3 沈殿槽
17 濁度計
W 原水
1 Raw water pit 2 Thickener 3 Sedimentation tank
17 Turbidimeter W Raw water

Claims (2)

上流に原水を断続供給する原水ピットを設けると共に、下流に凝集剤を添加して原水からフロックを沈降分離させるシックナーを設けた一連の配管経路中にシックナーに比し小型で内部に撹拌装置を設けた沈殿槽を設け、該沈殿槽は、その上流側の側壁下部に原水ピットの下流側の側壁下部に水平配管を介して上流側の側壁上方部位を接続すると共に、複数の阻流板を上下で食い違いに内部配置した垂直配管の下流側の側壁下部を配管接続し、沈殿槽の下流側の側壁上方にシックナーの上流側の側壁上方を配管接続し、沈殿槽の底部は傾斜配管を介してシックナーの上流側の側壁下部に連結して成り、沈殿槽内の原水の濁度を計測し、その濁度に基づき前記垂直配管上端に設けた投入口から投入される凝集剤の添加量を調整することを特徴とする原水への凝集剤添加量調整方法。 Raw water with the provision of the intermittent supplying raw water pit upstream, provided with a stirrer therein small compared to the thickener in a series of piping channel in which a thickener for sedimentation of the flocs from the raw water by adding a flocculant downstream The sedimentation tank is connected to the upstream side wall lower part of the upstream side wall via the horizontal pipe to the downstream side wall lower part of the upstream side of the raw water pit. The lower side wall of the vertical pipe arranged in a staggered manner is connected to the lower side of the vertical pipe, the upper side wall of the thickener is connected to the upper side of the downstream of the settling tank, and the bottom of the settling tank is connected to the bottom of the settling tank via an inclined pipe. It is connected to the lower part of the side wall on the upstream side of the thickener, measures the turbidity of the raw water in the sedimentation tank, and adjusts the amount of flocculant added from the inlet provided at the upper end of the vertical pipe based on the turbidity To be characterized by That flocculant amount adjusting method of the raw water. 上流に原水を断続供給する原水ピットを設けると共に、下流に凝集剤を添加して原水からフロックを沈降分離させるシックナーを設けた一連の配管経路中にシックナーに比し小型で内部に撹拌装置を設けた沈殿槽を設け、該沈殿槽は、その上流側の側壁下部に原水ピットの下流側の側壁下部に水平配管を介して上流側の側壁上方部位を接続すると共に、複数の阻流板を上下で食い違いに内部配置した垂直配管の下流側の側壁下部を配管接続し、沈殿槽の下流側の側壁上方にシックナーの上流側の側壁上方を配管接続し、沈殿槽の底部は傾斜配管を介してシックナーの上流側の側壁下部に連結し、沈殿槽内に濁度計を設け、該濁度計で計測された濁度に基づき添加量が調整される凝集剤の投入口を前記垂直配管上端に設けたことを特徴とする原水処理装置。 Raw water with the provision of the intermittent supplying raw water pit upstream, provided with a stirrer therein small compared to the thickener in a series of piping channel in which a thickener for sedimentation of the flocs from the raw water by adding a flocculant downstream The sedimentation tank is connected to the upstream side wall lower part of the upstream side wall via the horizontal pipe to the downstream side wall lower part of the upstream side of the raw water pit. The lower side wall of the vertical pipe arranged in a staggered manner is connected to the lower side of the vertical pipe, the upper side wall of the thickener is connected to the upper side of the downstream of the settling tank, and the bottom of the settling tank is connected to the bottom of the settling tank via an inclined pipe. Connected to the lower part of the side wall on the upstream side of the thickener, a turbidity meter is provided in the settling tank, and the inlet of the flocculant whose addition amount is adjusted based on the turbidity measured by the turbidimeter is located at the upper end of the vertical pipe Hara characterized by the establishment Processing apparatus.
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JPS583723B2 (en) * 1978-07-05 1983-01-22 株式会社日立製作所 Agglomeration effect detection device
JPS60175508A (en) * 1984-02-21 1985-09-09 Kurita Water Ind Ltd Flocculation reaction apparatus
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JPH06289007A (en) * 1993-04-02 1994-10-18 Kurita Water Ind Ltd Device for determining flocculation property of flocculation flock
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