JP3303723B2 - Coagulation treatment equipment - Google Patents
Coagulation treatment equipmentInfo
- Publication number
- JP3303723B2 JP3303723B2 JP10300697A JP10300697A JP3303723B2 JP 3303723 B2 JP3303723 B2 JP 3303723B2 JP 10300697 A JP10300697 A JP 10300697A JP 10300697 A JP10300697 A JP 10300697A JP 3303723 B2 JP3303723 B2 JP 3303723B2
- Authority
- JP
- Japan
- Prior art keywords
- partition plate
- chamber
- stirring
- passage
- treatment tank
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Description
【0001】[0001]
【発明の属する技術分野】この発明は、原水中の懸濁物
質(SSとも記す。)を固液分離する際、SSを凝集反
応により均一で大きな凝集汚泥(フロック)にして沈殿
させるための凝集処理装置に関する。BACKGROUND OF THE INVENTION The present invention relates to an agglomeration method for solidifying a suspended solid (also referred to as SS) in raw water into solid and liquid flocculated sludge by flocculation reaction. It relates to a processing device.
【0002】[0002]
【従来の技術】原水の供給路と、処理水の取出路とを有
する凝集処理槽の内部で、処理水量、滞溜時間、原水中
のSSの性状等に応じ、SSをフロックに生成するのに
最適な攪拌羽根を選択して回転駆動することは従来から
公知である。2. Description of the Related Art In a flocculation treatment tank having a feed path for raw water and a discharge path for treated water, SS is formed into flocs in accordance with the amount of treated water, the residence time, the properties of SS in the raw water, and the like. It is conventionally known to select an optimal stirring blade and to rotate the stirring blade.
【0003】[0003]
【発明が解決しようとする課題】処理槽内でSSが凝集
反応によりフロックに生長すると大きな沈降速度で槽底
に沈降し、水中に残溜する未反応のSSの生長が抑制さ
れるため、槽内のフロックの全体がSSと一緒に浮遊す
るような強い攪拌を攪拌羽根で行わねばならない。その
結果、SSが相互衝突により粗大化してフロックになる
一方で、粗大化したフロックが攪拌羽根と衝突して破砕
されるという相反した現象が生じ、均一で、大きなフロ
ックが得られない。又、強い攪拌によって処理槽に流入
した原水が出口路にショートパスし、フロックが生長し
ないまゝ沈殿槽に流入するため、沈殿槽での固液の沈殿
分離が充分に行われず、沈殿槽の出口路からはSSが混
入した水質の悪い処理水が流出する。When SS grows into flocs due to an agglutination reaction in the treatment tank, it sinks to the bottom of the tank at a high sedimentation speed, and the growth of unreacted SS remaining in water is suppressed. Strong stirring must be performed by the stirring blade so that the entire floc inside floats together with the SS. As a result, the SSs are coarsened by the mutual collision to become flocs, while the coarsened flocs collide with the stirring blades and are crushed, so that a contradictory phenomenon occurs, and a uniform and large floc cannot be obtained. In addition, raw water that has flowed into the treatment tank due to strong agitation is short-passed to the outlet path and flows into the sedimentation tank until floc does not grow. From the exit, treated water of poor quality mixed with SS flows out.
【0004】[0004]
【課題を解決するための手段】本発明は上述した問題点
を解消するために開発されたのであって、凝集処理装置
として、凝集処理槽と、液及び沈殿物が通過する通路を
備え、上記凝集処理槽の内部を上下方向の複数の室に区
分する複数の仕切板と、上記仕切板で区分された夫々の
室の内部を攪拌する攪拌手段と、凝集処理槽の内部に原
水を上下方向に通水して処理水を取出すため該処理槽の
上下一方の端部に設けられた原水の供給路と、他方の端
部に設けられた処理水の取出路とからなり、上記仕切板
の通路は夫々扇形で、上段の室の仕切板の通路と、下段
の室の仕切板の通路とには位相を保たせ、両通路を流れ
る水を短絡させることがないようにしたことを特徴とす
る。SUMMARY OF THE INVENTION The present invention has been developed to solve the above-mentioned problems. The present invention provides an agglomeration treatment apparatus comprising an agglomeration treatment tank and a passage through which a liquid and a sediment pass. A plurality of partition plates for dividing the inside of the coagulation treatment tank into a plurality of vertical chambers; a stirring means for stirring the interior of each of the compartments divided by the partition plate; And a treated water supply passage provided at one of the upper and lower ends of the treatment tank, and a treated water take-out passage provided at the other end of the treatment tank. The passages are fan-shaped, and the passage of the partition plate in the upper chamber and the passage of the partition plate in the lower chamber are kept in phase, so that the water flowing through both passages is not short-circuited. I do.
【0005】[0005]
【発明の実施の形態】上記仕切板は攪拌羽根を備え、仕
切板は中心を回転軸に固定されて回転駆動されるように
してもよいし、仕切板を凝集処理槽の内壁に固定し、こ
の仕切板の中心部を緩く貫通して回転駆動される回転軸
に仕切板上で回転駆動される攪拌羽根を設けてもよい。
又、上記処理槽の下端には沈殿物の排出路を設けてもよ
い。DETAILED DESCRIPTION OF THE INVENTION The partition plate is provided with a stirring blade, Specification
The cutting plate may be fixed at the center to the rotation shaft and driven to rotate, or the partition plate may be fixed to the inner wall of the coagulation treatment tank, and the partition plate is gently penetrated through the center to rotate. axis
The stirring blade is rotated on a partition plate may be provided.
Further, a discharge path for sediment may be provided at the lower end of the processing tank.
【0006】[0006]
【実施例】図示の各実施例において、10は凝集処理
槽、11は液及び沈殿物(汚泥)が通過する通路12を
備え、上記処理槽の内部を上下方向の複数の室13に区
分する仕切板、14は上記仕切板で区分された夫々の室
13内を攪拌する攪拌手段を示し、攪拌手段は凝集処理
槽の中心に沿って垂下し、モータMによって回転駆動さ
れる回転軸15と、回転軸の回転で水平に旋回する攪拌
羽根16とからなり、攪拌羽根は高さ5〜10cmの板
状、又は櫛状のパドル形で、水平に旋回する周速は10
〜100cm/秒程度である。DESCRIPTION OF THE PREFERRED EMBODIMENTS In each of the illustrated embodiments, reference numeral 10 denotes a coagulation treatment tank, 11 a passage 12 through which a liquid and a sediment (sludge) pass, and the inside of the treatment tank is divided into a plurality of vertical chambers 13. The partition plates 14 show stirring means for stirring the inside of each of the chambers 13 divided by the partition plate. The stirring means hangs down along the center of the coagulation treatment tank, and the rotating shaft 15 is driven to rotate by the motor M. And a stirring blade 16 that rotates horizontally by rotation of a rotating shaft. The stirring blade is a plate-shaped or comb-shaped paddle having a height of 5 to 10 cm.
About 100 cm / sec.
【0007】凝集処理槽の槽高、及び直径は、原水中に
含まれているSSの濃度に応じ適切に定めるが、攪拌羽
根の高さ5〜10cmに対して仕切板で区分された室1
3の高さは約20〜50cmが好ましい。The tank height and diameter of the coagulation tank are appropriately determined according to the concentration of SS contained in the raw water, but the height of the stirring blade is 5 to 10 cm and the chamber 1 is divided by a partition plate.
The height of 3 is preferably about 20 to 50 cm.
【0008】仕切板11に設ける通路12は開き角30
〜90°の扇形で、2枚、或いはそれ以上の数の仕切板
によって凝集処理槽内を上下方向の三室以上に区分する
ときは上段の仕切板の通路12と、下段の仕切板の通路
12に180°の位相をもたせる(図1B,図4B参
照)。図示の各実施例では仕切板11を上下方向に5段
設け、凝集処理槽の内部を上下方向の6室に区分してあ
る。The passage 12 provided in the partition plate 11 has an opening angle 30
When the inside of the agglomeration treatment tank is divided into three or more chambers in the vertical direction by two or more partitions in a sector shape of up to 90 °, the passage 12 of the upper partition and the passage 12 of the lower partition are provided. Have a phase of 180 ° (see FIGS. 1B and 4B). In each of the illustrated embodiments, the partition plate 11 is provided in five stages in the vertical direction, and the inside of the coagulation treatment tank is divided into six chambers in the vertical direction.
【0009】凝集処理槽の内部に原水を上下方向に通水
して処理水を取出すため、原水を下向流で通水するとき
は最上段の室13Aに原水を供給する供給路17、最下
段の室13Bに処理水を取出す取出路18を設ける。
又、原水を上向流で通水するときは、破線で示したよう
に最下段の室13Bに原水を供給する供給路17、最上
段の室13Aに処理水を取出す取出路18を設ける。そ
して、最下段の室の底には沈殿物(凝集汚泥)の排出路
19を設ける。尚、供給路17に供給する原水には予め
凝集剤が添加してある。When raw water is passed in a downward flow, the raw water is supplied to the uppermost chamber 13A through the supply passage 17 for supplying the raw water to the upper chamber 13A in order to extract the treated water by flowing the raw water vertically into the coagulation treatment tank. An extraction path 18 for extracting treated water is provided in the lower chamber 13B.
When the raw water flows in the upward flow, a supply path 17 for supplying the raw water to the lowermost chamber 13B and an extraction path 18 for taking out the treated water to the uppermost chamber 13A are provided as shown by broken lines. A discharge path 19 for sediment (coagulated sludge) is provided at the bottom of the lowermost chamber. Note that a coagulant is added to the raw water supplied to the supply path 17 in advance.
【0010】図1に示した実施例では攪拌手段14の回
転軸15に各仕切板11の中心を固定し、仕切板は回転
軸15と一体に水平に回転するようにしてある。そし
て、扇形の通路13の半径方向の直線縁部を上や下に直
角に折り曲げたり、仕切板の上面や下面に半径方向に溶
接するなどして攪拌羽根16を設けてある(図1C参
照)。尚、仕切板11の外周と、処理槽の内周との間に
は0.5〜2cm程度の間隙を形成する。In the embodiment shown in FIG. 1, the center of each partition plate 11 is fixed to the rotating shaft 15 of the stirring means 14, and the partition plate is rotated integrally with the rotating shaft 15 horizontally. Then, the stirring blade 16 is provided by bending the straight edge portion in the radial direction of the fan-shaped passage 13 upward or downward at right angles, or by welding the upper and lower surfaces of the partition plate in the radial direction (see FIG. 1C). . Note that a gap of about 0.5 to 2 cm is formed between the outer periphery of the partition plate 11 and the inner periphery of the processing tank.
【0011】処理を行うには、回転軸15と一体に全部
の仕切板11を水平回転させ、槽内に下向流で通水する
ときは最上段の室13Aに凝集剤が添加された原水を供
給する。全部の仕切板11は一体として回転するため、
上段の仕切板の通路12と下段の仕切板12の通路12
は180°の位相を保っているので、水は短絡すること
なく矢印で示したように上の室から下の室に順番に流下
し、各室内で仕切板と一体に旋回する攪拌羽根16の攪
拌作用により凝集反応を起こし、SSは次第に凝集して
フロックに成長する。そして、攪拌羽根により強力な攪
拌は必要がないため、フロックは破壊されることがな
い。このようにして、凝集槽として働く場合は、大きく
均一なフロックを含む水は、取出路18から取出し、後
段の沈殿槽等の処理手段へ供給する。又、最下段の室1
3Bの底に砂利などを含む沈降性に富むフロックが沈降
する場合は、排出路19から定期的に、或いは連続的に
排出する。In order to perform the treatment, all the partition plates 11 are horizontally rotated integrally with the rotating shaft 15, and when water flows downward in the tank, the raw water containing coagulant is added to the uppermost chamber 13A. Supply. Since all the partition plates 11 rotate integrally,
Passage 12 of upper partition plate and passage 12 of lower partition plate 12
Keeps the phase of 180 °, so that the water flows down from the upper chamber to the lower chamber in order as shown by the arrow without short-circuiting, and the stirring blades 16 which rotate integrally with the partition plate in each chamber are shown. An agglutination reaction is caused by the stirring action, and the SS gradually aggregates and grows into flocs. And since strong stirring is not required by the stirring blade, the floc is not destroyed. In this way, when acting as a flocculation tank, water containing large and uniform flocs is taken out from the take-out channel 18 and supplied to a processing means such as a sedimentation tank at the subsequent stage. Also, the lowermost room 1
In the case where floc containing sedimentation, such as gravel, settles on the bottom of 3B, the floc is discharged from the discharge path 19 periodically or continuously.
【0012】又、回転軸15と一体に全部の仕切板11
を水平回転させ、槽内に上向流で通水するときは、最下
段の室13Bに凝集剤が添加された原水を供給する。全
部の仕切板11は一体として回転するため、上段の仕切
板の通路12と下段の仕切板12の通路12は180°
の位相を保っているので、水は短絡することなく下の室
から上の室に順番に上昇し、各室内で仕切板と一体に旋
回する攪拌羽根16の攪拌作用により凝集反応を起こ
し、SSは次第に凝集してフロックに成長する。そし
て、攪拌羽根により強力な攪拌は必要がないため、フロ
ックは破壊されることがない。そして、フロックが大き
く成長し、上向流する水流に抗して仕切板の通路を自重
で下降できる場合は、そのフロックは順番に上の室から
下の室に移動し、最終的に最下段の室13Bの底に均一
な大きさで沈降し、反応槽底部から最大で反応槽の高さ
の半分程度まで汚泥ゾーンを生成する。汚泥ゾーンの高
さがそれ以上高まったら汚泥ゾーンの余分な汚泥は排出
路19から定期的に、或いは連続的に排出する。そし
て、汚泥ゾーンによりSSを除去された処理水は最上段
の室13Aに設けた取出路18から取出す。又、フロッ
クによる汚泥ゾーンを生成しない場合は、大きく均一な
フロックを含む処理水として取出路18から取出し、後
段の沈殿槽等の処理手段へ供給する。Further, all the partition plates 11 are integrally formed with the rotating shaft 15.
Is rotated horizontally, and when water flows in the tank in an upward flow, the raw water to which the coagulant is added is supplied to the lowermost chamber 13B. Since all the partition plates 11 rotate integrally, the passage 12 of the upper partition plate and the passage 12 of the lower partition plate 12 are 180 °.
, The water rises in order from the lower chamber to the upper chamber without short-circuiting, and causes a coagulation reaction due to the stirring action of the stirring blade 16 which turns integrally with the partition plate in each chamber. Gradually aggregates and grows into flocs. And since strong stirring is not required by the stirring blade, the floc is not destroyed. If the flock grows significantly and can descend the path of the partition plate by its own weight against the upward flowing water, the flock moves from the upper chamber to the lower chamber in order, and finally the lowermost Settles at the bottom of the chamber 13B with a uniform size, and generates a sludge zone from the bottom of the reactor up to about half the height of the reactor. When the height of the sludge zone is further increased, excess sludge in the sludge zone is discharged from the discharge passage 19 periodically or continuously. Then, the treated water from which the SS has been removed by the sludge zone is extracted from the extraction passage 18 provided in the uppermost chamber 13A. When the sludge zone is not generated by flocs, it is taken out from the discharge passage 18 as treated water containing large and uniform flocs, and supplied to a processing means such as a sedimentation tank at the subsequent stage.
【0013】原水中のSSの性状によっては仕切板11
上に沈積し、水の流れを乱したり、その重さで仕切板が
変形することもある。これを防止するには、図2に示す
ように攪拌羽根16は仕切板11の下面に下向きに設け
ると共に、仕切板の上面から上に0.5〜2cm程度離
し、回転軸を避けた直径方向の棒材、角材からなる掻き
寄せ部材20の両端部を処理槽の内壁に固定し、回転す
る仕切板上に沈積する汚泥を上記掻き寄せ部材20で通
路12から下の段の仕切板上に落下させるようにする。
又、図3(A)や(B)に示すように仕切板11を凸又
は凹の円錐形にし、その上面に汚泥が沈積するのを防止
するようにしてもよい。Depending on the nature of the SS in the raw water, the partition plate 11
It can accumulate on top and disrupt the flow of water, and the weight can deform the divider. In order to prevent this, as shown in FIG. 2, the stirring blade 16 is provided downward on the lower surface of the partition plate 11 and is separated from the upper surface of the partition plate by about 0.5 to 2 cm in the diametrical direction avoiding the rotation axis. The both ends of the scraping member 20 made of a bar and a square are fixed to the inner wall of the processing tank, and the sludge deposited on the rotating partition plate is separated from the passage 12 by the scraping member 20 onto the lower partition plate. Let it fall.
Alternatively, as shown in FIGS. 3A and 3B, the partition plate 11 may have a convex or concave conical shape to prevent sludge from depositing on the upper surface thereof.
【0014】図4は、各仕切板11の外周を処理槽10
の内壁に固定し、攪拌手段14の回転軸15は仕切板の
中心孔を緩く貫通して垂下する。そして、回転軸15に
は仕切板の上面から上に0.5〜2cm程度、離れて水
平に旋回する攪拌羽根16が放射状に複数本、取付けて
ある。FIG. 4 shows the outer periphery of each partition plate 11 in the processing tank 10.
And the rotating shaft 15 of the agitating means 14 hangs loosely through the center hole of the partition plate. A plurality of agitating blades 16 are provided on the rotating shaft 15 in a radial manner so as to rotate horizontally about 0.5 to 2 cm apart from the upper surface of the partition plate.
【0015】処理を行うには回転軸の回転で攪拌羽根1
6を旋回させ、槽内に下向流で通水するときは最上段の
室13Aに凝集剤が添加された原水を供給する。上段の
仕切板の通路12と、下段の仕切板の通路12は180
°の位相を保っているので、水は短絡することなく矢印
で示したように上の室から下の室に順番に流下し、各室
内で旋回する攪拌羽根16の攪拌作用により凝集反応を
起こし、SSは次第に凝集してフロックに成長する。そ
して、攪拌羽根による強力な攪拌は必要がないため、フ
ロックは破壊されることがない。このようにして、凝集
槽として働く場合は、大きく均一なフロックを含む水は
取出路18から取出し、後段の沈殿槽等の処理手段へ供
給する。又、最下段の室13Bの底に砂利などを含む沈
降性に富むフロックが沈降する場合は、排出路19から
定期的に、或いは連続的に排出する。又、SSを除去さ
れた処理水は取出路18から取出す。In order to perform the processing, the stirring blade 1 is rotated by rotating the rotating shaft.
When the water 6 is swirled and water flows downward in the tank, the raw water to which the coagulant has been added is supplied to the uppermost chamber 13A. The path 12 of the upper partition plate and the path 12 of the lower partition plate are 180
°, the water flows down from the upper chamber to the lower chamber in order as shown by the arrow without short-circuiting, and the agitation action of the stirring blades 16 rotating in each chamber causes an agglutination reaction. , SS gradually aggregate and grow into flocs. And since strong stirring by the stirring blade is not required, the flocks are not destroyed. In this way, when acting as a flocculation tank, water containing large and uniform flocs is taken out from the take-out channel 18 and supplied to a processing means such as a sedimentation tank at the subsequent stage. Further, when flocs having a high sedimentation property including gravel settle on the bottom of the lowermost chamber 13B, the flocs are discharged from the discharge path 19 periodically or continuously. Further, the treated water from which SS has been removed is taken out from the take-out passage 18.
【0016】回転軸の回転で攪拌羽根を旋回させ、槽内
に上向流で通水するときは、最下段の室13Bに凝集剤
が添加された原水を供給する。上段の仕切板の通路12
と、下段の仕切板の通路12は180°の位相を保って
いるので、水は短絡することなく下の室から上の室に順
番に上昇し、各室内で旋回する攪拌羽根16の攪拌作用
により凝集反応を起こし、SSは次第に凝集してフロッ
クに成長する。そして、攪拌羽根による強力な攪拌は必
要がないため、フロックは破壊されることがない。そし
て、フロックが大きく成長し、上向流する水流に抗して
仕切板の通路を自重で下降できる場合は、そのフロック
は順番に上の室から下の室に移動し、最終的に最下段の
室13Bの底に均一な大きさで沈降し、反応槽底部から
最大で反応槽の高さの半分程度まで汚泥ゾーンを生成す
る。汚泥ゾーンの高さがそれ以上高まったら汚泥ゾーン
の余分な汚泥は排出路19から定期的に、或いは連続的
に排出する。そして、汚泥ゾーンによりSSを除去され
た処理水は最上段の室13Aに設けた取出路18から取
出す。又、フロックによる汚泥ゾーンを生成しない場合
は、大きく均一なフロックを含む処理水として取出路1
8から取出し、後段の沈殿槽等の処理手段へ供給する。When the stirring blade is swirled by the rotation of the rotating shaft and water flows upward in the tank, raw water to which a coagulant has been added is supplied to the lowermost chamber 13B. Passage 12 of upper partition plate
And the passage 12 of the lower partition plate keeps the phase of 180 °, so that the water rises in order from the lower chamber to the upper chamber without short-circuiting, and the stirring action of the stirring blades 16 rotating in each chamber. Causes an aggregation reaction, and the SS gradually aggregates and grows into flocs. And since strong stirring by the stirring blade is not required, the flocks are not destroyed. If the flock grows significantly and can descend the path of the partition plate by its own weight against the upward flowing water, the flock moves from the upper chamber to the lower chamber in order, and finally the lowermost Settles at the bottom of the chamber 13B with a uniform size, and generates a sludge zone from the bottom of the reactor up to about half the height of the reactor. When the height of the sludge zone is further increased, excess sludge in the sludge zone is discharged from the discharge passage 19 periodically or continuously. Then, the treated water from which the SS has been removed by the sludge zone is extracted from the extraction passage 18 provided in the uppermost chamber 13A. When the sludge zone is not generated by the floc, the treated water containing the large and uniform floc is taken out of the discharge path 1.
8 and supplied to processing means such as a sedimentation tank at the subsequent stage.
【0017】[0017]
【発明の効果】以上で明らかなように本発明によれば、
仕切板で区分された凝集処理槽の上下方向の複数の室を
原水が下向流、又は上向流で通水する際、上段の室の仕
切板の通路と下段の室の仕切板の通路は位相を保って連
通しないので、水は短絡することなく上の室から下の室
に順番に下降し、又は下の室から上の室に順番に上昇
し、各室内で旋回する攪拌羽根の攪拌作用を受けて効果
的に凝集反応を行い、原水中のSSは均一で大きなフロ
ックに生長する。上向流で、且つ汚泥ゾーンを清々する
ようなフロックが選られる場合は、フロックは槽底に沈
降し、原水が汚泥ゾーンを通過することにより充分に固
液分離を行うことができる。そして、大きなフロックは
沈降速度が大であるため、凝集処理槽を小型化できる。
更に、充分に固液分離が行われるため、キャリーオーバ
ーし易い小さなフロックが少なく、清澄な処理水が得ら
れる。As apparent from the above, according to the present invention,
When raw water flows downward or upward through a plurality of vertical chambers of the coagulation treatment tank separated by a partition plate , the upper chamber
The passage of the cutting plate and the passage of the partition plate of the lower chamber are connected in phase.
Water does not pass through, so water does not short-circuit from the upper chamber to the lower chamber.
Descend sequentially, or ascend from lower chamber to upper chamber
Then , the flocculation reaction is effectively performed by the stirring action of the stirring blades rotating in each room, and the SS in the raw water grows into uniform and large flocs. In the case where a floc that is upward flowing and that makes the sludge zone clear is selected, the floc settles at the bottom of the tank, and the solid water can be sufficiently separated by the raw water passing through the sludge zone. And since a large floc has a high sedimentation speed, the coagulation treatment tank can be miniaturized.
Further, since the solid-liquid separation is sufficiently performed, there are few small flocs which are liable to carry over, and clear treated water can be obtained.
【図1】(A)は本発明の凝集処理装置の第1実施例の
縦断面図、(B)は図1(A)のB−B線での断面図、
(C)は要部の欠截斜視図である。1A is a longitudinal sectional view of a first embodiment of the coagulation processing apparatus of the present invention, FIG. 1B is a sectional view taken along line BB of FIG. 1A,
(C) is a cutaway perspective view of a main part.
【図2】(A)は本発明の凝集処理装置の第2実施例の
一部の縦断面図、(B)は図2(A)のB−B線での断
面図である。FIG. 2A is a longitudinal sectional view of a part of a second embodiment of the coagulation apparatus of the present invention, and FIG. 2B is a sectional view taken along line BB of FIG. 2A.
【図3】(A)と(B)は図1,図2の実施例に使用可
能な仕切板の2例を示す断面図である。FIGS. 3A and 3B are cross-sectional views showing two examples of a partition plate that can be used in the embodiment shown in FIGS. 1 and 2;
【図4】(A)は本発明の凝集処理装置の更に他の一実
施例の縦断面図、(B)は図4(A)のB−B線での断
面図、(C)は要部の欠截斜視図である。4 (A) is a longitudinal sectional view of still another embodiment of the coagulation treatment apparatus of the present invention, FIG. 4 (B) is a sectional view taken along line BB of FIG. 4 (A), and FIG. It is a fragmentary perspective view of a part.
10 凝集処理槽 11 仕切板 12 仕切板の通路 13 仕切板で上下方向に区分された室 13A 最上段の室 13B 最下段の室 14 攪拌手段 15 攪拌手段の回転軸 16 攪拌手段の攪拌羽根 17 原水の供給路 18 処理水の取出路 19 沈殿物の排出路 20 掻き寄せ部材 REFERENCE SIGNS LIST 10 Coagulation treatment tank 11 Partition plate 12 Partition plate passage 13 Room divided vertically by partition plate 13A Uppermost chamber 13B Lowermost chamber 14 Stirring means 15 Rotating shaft of stirring means 16 Stirring blades of stirring means 17 Raw water Supply path 18 treated water removal path 19 sediment discharge path 20 scraping member
Claims (3)
通路を備え、上記凝集処理槽の内部を上下方向の複数の
室に区分する複数の仕切板と、上記仕切板で区分された
夫々の室の内部を攪拌する攪拌手段と、凝集処理槽の内
部に原水を上下方向に通水して処理水を取出すため該処
理槽の上下一方の端部に設けられた原水の供給路と、他
方の端部に設けられた処理水の取出路とからなり、上記
仕切板の通路は夫々扇形で、上段の室の仕切板の通路
と、下段の室の仕切板の通路とには位相を保たせ、両通
路を流れる水を短絡させることがないようにしたことを
特徴とする凝集処理装置。An agglomeration treatment tank, a plurality of partitions provided with a passage through which a liquid and a sediment pass, and a plurality of partition plates for dividing the inside of the agglutination treatment tank into a plurality of vertical chambers, and the partition plate A stirring means for stirring the inside of each chamber, and a raw water supply passage provided at one of the upper and lower ends of the treatment tank for extracting the treated water by vertically flowing the raw water into the coagulation treatment tank. And a discharge path for treated water provided at the other end.
The passages of the dividers are fan-shaped, and the passages of the dividers in the upper chamber
And the passage of the partition plate in the lower chamber
An agglomeration treatment apparatus characterized in that water flowing in a road is not short-circuited .
て、仕切板は攪拌羽根を備え、仕切板は中心を回転軸に
固定されて回動駆動されるようになっていることを特徴
とする凝集処理装置。2. The coagulation treatment apparatus according to claim 1, wherein the partition plate has stirring blades, and the partition plate has a center at a rotation axis.
An agglomeration processing apparatus, which is fixed and driven to rotate.
て、仕切板を凝集処理槽の内壁に固定し、この仕切板の
中心部を緩く貫通して回転駆動される回転軸に仕切板上
で回転駆動される攪拌羽根を設けたことを特徴とする凝
集処理装置。3. The coagulation treatment apparatus according to claim 1, wherein the partition plate is fixed to an inner wall of the coagulation treatment tank .
An agglomeration treatment apparatus, wherein a stirring shaft rotatably driven on a partition plate is provided on a rotating shaft that is rotatably driven through a central portion loosely .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10300697A JP3303723B2 (en) | 1997-04-09 | 1997-04-21 | Coagulation treatment equipment |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9-90704 | 1997-04-09 | ||
JP9070497 | 1997-04-09 | ||
JP10300697A JP3303723B2 (en) | 1997-04-09 | 1997-04-21 | Coagulation treatment equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH10337406A JPH10337406A (en) | 1998-12-22 |
JP3303723B2 true JP3303723B2 (en) | 2002-07-22 |
Family
ID=26432156
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10300697A Expired - Fee Related JP3303723B2 (en) | 1997-04-09 | 1997-04-21 | Coagulation treatment equipment |
Country Status (1)
Country | Link |
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JP (1) | JP3303723B2 (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19938818A1 (en) * | 1999-08-19 | 2001-02-22 | Envicon Klaertech Verwalt | Small, aerobic waste water treatment plant especially suitable for hot fatty effluent from fast food restaurants, has special provision for addition and mixing of flocculating additives |
JP4142321B2 (en) * | 2002-03-29 | 2008-09-03 | 住友重機械エンバイロメント株式会社 | Coagulation sedimentation equipment |
JP4711074B2 (en) * | 2006-03-29 | 2011-06-29 | 栗田工業株式会社 | Aggregation reactor |
JP4743421B2 (en) * | 2006-03-29 | 2011-08-10 | 栗田工業株式会社 | Aggregation reactor |
JP4711075B2 (en) * | 2006-03-29 | 2011-06-29 | 栗田工業株式会社 | Aggregation reactor |
JP5627782B2 (en) * | 2010-07-30 | 2014-11-19 | イー・エム・デイー・ミリポア・コーポレイシヨン | Disposable vortex prevention device |
CN111559811A (en) * | 2019-11-21 | 2020-08-21 | 新昌县恒益塑料厂 | Environment-friendly treatment method applied to plastic production process |
-
1997
- 1997-04-21 JP JP10300697A patent/JP3303723B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
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JPH10337406A (en) | 1998-12-22 |
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