JPS62258714A - Apparatus for purifying suspension by sedimentation - Google Patents

Apparatus for purifying suspension by sedimentation

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Publication number
JPS62258714A
JPS62258714A JP10161686A JP10161686A JPS62258714A JP S62258714 A JPS62258714 A JP S62258714A JP 10161686 A JP10161686 A JP 10161686A JP 10161686 A JP10161686 A JP 10161686A JP S62258714 A JPS62258714 A JP S62258714A
Authority
JP
Japan
Prior art keywords
water
raw water
spiral
suspended
chamber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP10161686A
Other languages
Japanese (ja)
Inventor
Masahiro Takeda
武田 正博
Kenjiro Takeda
武田 憲治郎
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
O H L KK
Original Assignee
O H L KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by O H L KK filed Critical O H L KK
Priority to JP10161686A priority Critical patent/JPS62258714A/en
Publication of JPS62258714A publication Critical patent/JPS62258714A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To efficiently sediment and concentrate the suspended component in raw water, by providing a water stream deflecting means for setting introduced raw water to a horizontal direction at the central part of a spiral water channel. CONSTITUTION:Turbid raw water flows in a tank from the introducing pipe 8 set to the central part of a spiral partition plate 5 to fill a clarifying chamber 1a but, at this time, the inflow energy of raw water is turned to a horizontal direction by a water stream deflecting means due to a spiral bottom plate 9a to push out the whole of raw water in a spiral water channel in a stable state. In a process allowing raw water to flow through the spiral water channel partitioned by a long flow passage, the suspended substance in raw water falls linearily to an oblique direction to be sedimented and concentrated in a concn. chamber 1b and is taken out to the outside from the discharge port 2 of the bottom part by valve operation. The clarified water in raw water from which the suspended substance was removed rises in the clarifying chamber 1a by rearward push-out force and floods over the zigzag weir 3 formed to the outer periphery of the clarifying chamber 1a to be gathered to a water gathering tub 4 and is taken out from a lead-out port 10.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は一般工場等より排出される懸濁水を濃縮懸濁成
分と清澄水に連続的に分離して取出すす沈降浄化装置の
改良に関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to an improvement in a sedimentation purification device that continuously separates and extracts suspended water discharged from general factories into concentrated suspended components and clear water.

〔背景技術〕[Background technology]

工場排水等の懸濁原水を沈澱させて′#4.濁成分と清
澄水に分^■する装置として、沈澱槽上部の清澄室に渦
巻き状の水路仕切板を設け。渦巻°き中心部から導入し
た原水を該渦巻水路に沿って流動させながら原水中の懸
濁物質を下方の濃縮室に沈降させるようにした装置が知
られている。
Precipitate suspended raw water such as factory wastewater'#4. A spiral waterway partition plate is installed in the clarification chamber above the settling tank as a device to separate turbid components and clear water. A device is known in which suspended solids in the raw water are allowed to settle in a concentration chamber below while the raw water introduced from the center of the swirl is made to flow along the swirl channel.

従来のこの種装置は渦巻き水路仕切板の外側端縁を槽内
壁に接続させているため水路の巾が不均等になり、且つ
水路先端が閉塞されるため滞留及び逆流等が生ずる。そ
の結果一旦沈降した懸濁物が巻き上げられて再び)脈濁
をおこし、゛清澄水のまま取出すことができないという
致命的な問題があった。また、槽内に導入した原水を水
平方向に押し出す方向性付与手段が考慮されていないた
め、バランスの良い流動が得られず、沈澱作用の効率を
低下させていた。
In conventional devices of this kind, the outer edge of the spiral waterway partition plate is connected to the inner wall of the tank, so the width of the waterway becomes uneven, and the tip of the waterway is blocked, resulting in stagnation and backflow. As a result, the suspended matter that had once settled would be stirred up and cause turbidity (again), resulting in the fatal problem that it was impossible to take out the water as clear water. Furthermore, since no consideration was given to a means for imparting directionality to push the raw water introduced into the tank in a horizontal direction, a well-balanced flow could not be obtained, reducing the efficiency of the settling action.

本発明の目的は清澄室の原水に安定した流動エネルギー
を与えるとともに、よどみや逆流による再)g濁を解消
した沈降浄化装置を提供することにある。
An object of the present invention is to provide a sedimentation purification device that provides stable flow energy to raw water in a clarification chamber and eliminates turbidity caused by stagnation and backflow.

〔発明の概要〕[Summary of the invention]

上記目的を達成するために、本発明は、円筒状の清澄室
の下方にスラッジ取出部を有するコーン状の濃縮室を一
体に連設した沈澱槽の清澄室内に、一連の渦巻き状水路
仕切板を、その外側端縁と清澄室内壁との間に水路を形
成するように離隔させて垂直に配設するとともに、水路
仕切板の渦巻き中心部に懸濁原水の導入管を垂直に挿入
し、さらに、水路仕切板の渦巻き中心部に、清澄室内の
導入原水を水平方向に向けて押し出すための水流偏向手
段を設けたものである。
In order to achieve the above object, the present invention provides a series of spiral waterway partition plates in the clarification chamber of a settling tank which is integrally connected with a cone-shaped concentration chamber having a sludge extraction section below the cylindrical clarification chamber. are spaced apart and vertically arranged so as to form a waterway between the outer edge and the wall of the clarification chamber, and an inlet pipe for suspended raw water is vertically inserted into the spiral center of the waterway partition plate, Furthermore, a water flow deflection means is provided at the center of the swirl of the channel partition plate for pushing out the raw water introduced into the clarification chamber in the horizontal direction.

水流偏向手段は、例えば、水路仕切板の渦巻き中心部の
下部に設けた適当な長さの螺旋状、底板で構成してもよ
く、また、清澄室の原水の重心レヘルにおいて原水導入
管の導入口を水平方向に向けて設けた構成でもよい。
The water flow deflection means may be constructed of, for example, a spiral bottom plate of an appropriate length provided below the spiral center of the waterway partition plate, and the raw water introduction pipe is introduced at the center of gravity of the raw water in the clarification chamber. A configuration in which the mouth is oriented horizontally may also be used.

〔発明の実施例〕[Embodiments of the invention]

以下に、本発明の実施例を添付図面に基づいて説明する
Embodiments of the present invention will be described below with reference to the accompanying drawings.

第1図において、1は円筒状の清澄室1aの下方にテー
パー状に下降傾斜した内壁を有する濃縮室ibを一体に
連通させた沈澱槽である。この沈澱槽1は下端にスラッ
ジ排出口2を存するとともに、清澄室1aの上端周縁に
清澄水を溢水させて取出すジグザグ堰3を設けてあり、
さらに、清澄室1aの外周には集水桶4が取付けられて
いる。
In FIG. 1, reference numeral 1 denotes a sedimentation tank in which a concentration chamber ib having a tapered downwardly inclined inner wall is connected to the lower part of a cylindrical clarifying chamber 1a. This sedimentation tank 1 has a sludge discharge port 2 at the lower end, and a zigzag weir 3 for overflowing and taking out clarified water around the upper end of the clarification chamber 1a.
Furthermore, a water collection bucket 4 is attached to the outer periphery of the clarification chamber 1a.

沈澱槽1の清澄室1aは、処理する懸濁水(原水)の量
に応じた水面積と水深を有し、その内部には渦巻き状に
形成した一連の水路仕切板5が垂直に配設されている。
The clarification chamber 1a of the settling tank 1 has a water area and water depth according to the amount of suspended water (raw water) to be treated, and a series of spiral water channel partition plates 5 are vertically disposed inside the clarification chamber 1a. ing.

水路仕切板5は清澄室1aの下部から上部のジグザグ堰
3のやや上方まで延在する高さを存し、且つ清澄室1a
の直径をほぼ均等の水路11に区画する一連の渦巻き板
で構成されており、その外側端縁5′と清澄室1aの間
に水路6を形成するように間隔して清澄室la内に独立
に懸架されている。図の実施例では集水桶4に固定した
十字形ブラケット7に仕切板5の上部を結合して懸架し
ている。
The waterway partition plate 5 has a height extending from the bottom of the clarification chamber 1a to slightly above the zigzag weir 3 at the top, and
It consists of a series of spiral plates that divide the diameter into waterways 11 of approximately equal diameter, and are spaced apart so as to form a waterway 6 between the outer edge 5' and the clarification chamber 1a. is suspended. In the illustrated embodiment, the upper part of the partition plate 5 is connected to and suspended from a cross-shaped bracket 7 fixed to the water collection tank 4.

本発明の第一の特徴は渦巻き状水路仕切板5の外側端縁
5′を清澄室1aの内壁面の間を開放して水路6を形成
したことにあり、かくして、沈澱槽1の清澄室la内に
は渦巻き状水路仕切板5によって該仕切板5の渦巻き中
心部から清澄室1aの内周壁に至り、且つ清澄室1a内
周壁との間が完全に開放された一連の長い水路が形成さ
れている。
The first feature of the present invention is that the outer edge 5' of the spiral waterway partition plate 5 is opened between the inner wall surfaces of the clarification chamber 1a to form a waterway 6. In la, a series of long water channels are formed by the spiral waterway partition plate 5, which extend from the spiral center of the partition plate 5 to the inner peripheral wall of the clarification chamber 1a, and are completely open between the inner peripheral wall of the clarification chamber 1a. has been done.

清澄室1aの渦巻き仕切板5の中心部には槽1内にQ’
(Q原水を導入する導入管8が上方から挿入されている
Q' is placed in the center of the spiral partition plate 5 of the clarification chamber 1a in the tank 1.
(An introduction pipe 8 for introducing Q raw water is inserted from above.

この種の装置は槽内に導入した懸濁水を清澄室la内に
おいて上記渦巻き水路5を介して流動させる過程での)
U濁物質を下方の濃縮室1bに沈澱させ、清澄水と懸濁
物に分離するものであるが、懸濁成分を効率良く沈澱さ
せるには清澄室la内の原水に安定した流動エネルギー
を与える必要がある。このために、本発明では渦巻き水
路の中心部すなわち、原水導入部に、原水の流入エネル
ギーを横方向に変える水流偏向手段9が設けられている
This type of device is used during the process of flowing suspended water introduced into the tank through the spiral water channel 5 in the clarification chamber la)
U The turbid substances are precipitated in the lower concentrating chamber 1b and separated into clear water and suspended matter. In order to efficiently settle the suspended components, stable flow energy is given to the raw water in the clarification chamber la. There is a need. For this purpose, in the present invention, a water flow deflection means 9 is provided at the center of the spiral waterway, that is, at the raw water introduction part, to change the inflow energy of the raw water in the lateral direction.

この水流偏向手段9は、例えば第3図、第4図に示すよ
うに、渦巻き仕切板5の中心付近の下部に適当な旋回長
さく好ましくは1〜1.5廻わり)の螺旋状底板9aを
設けた構成でもよく、また、第5図のように原水導入管
8の導入口9bを清澄室1aの原水の重心位置(レヘル
)において横方向に向けて設けた構成でもよい。この場
合、清澄室の水の重心は通常、水面から水深の3分の2
の位置にあるので導入管8の先端をこの深さまで延ばし
、導入口9bを水平方向に向けて配設する。
As shown in FIGS. 3 and 4, for example, the water flow deflection means 9 is provided with a spiral bottom plate 9a having an appropriate swirl length (preferably 1 to 1.5 turns) at the lower part of the center of the spiral partition plate 5. Alternatively, as shown in FIG. 5, the inlet 9b of the raw water inlet pipe 8 may be oriented laterally at the center of gravity of the raw water in the clarification chamber 1a. In this case, the center of gravity of the water in the clarification chamber is usually two-thirds of the depth from the water surface.
Therefore, the tip of the introduction tube 8 is extended to this depth, and the introduction port 9b is arranged horizontally.

沈澱槽1は堆積した懸濁物質がその自重により濃縮され
、且つ排出されるように、濃縮室の内壁を排出口2に向
けてコーン状に下向1頃斜させである。
The sedimentation tank 1 has an inner wall inclined downward in a cone shape toward the discharge port 2 so that the accumulated suspended solids are concentrated by their own weight and discharged.

次に本発明の詳細な説明する。Next, the present invention will be explained in detail.

懸濁原水は渦巻き仕切板5の中心部にセントされた尋人
管8から槽内に流入し、清澄室1aに満たされるがその
際、原水の流入エネルギーは水流偏向手段9 (9a、
9b等)により、水平方向に向けられ、渦巻き水路内の
原水全体を安定した状態で外周方向へ押し出す。その結
果、清澄室la内の原水は、渦巻き水路に沿って外周に
向かう連続した押し出し流れとなって′a縮空室1b上
面をすべるようにして水平に流動する。そして、長い流
路に仕切られた渦巻き水路を流動する過程で、)懸濁物
は水路を斜め直線的に下降して濃縮室に沈−降、濃縮さ
れ、底部の排出口からバルブ操作あるいはスラッジポン
プなどにより外部に取出される。
Suspended raw water flows into the tank from a fathom pipe 8 placed in the center of the spiral partition plate 5, and fills the clarification chamber 1a.
9b etc.), it is directed horizontally and pushes out the entire raw water in the spiral waterway in a stable state toward the outer circumference. As a result, the raw water in the clarification chamber la becomes a continuous pushing flow toward the outer periphery along the spiral waterway, and flows horizontally as if sliding on the upper surface of the contraction chamber 1b. In the process of flowing through a spiral waterway partitioned into long channels, the suspended matter descends diagonally straight down the waterway, settles in the concentration chamber, and is concentrated. Extracted to the outside using a pump, etc.

他方、懸濁物質の除去された原水中の清澄水は後流の押
し出し力により清澄室la内を上昇し、清澄室1aの外
周に形成したジグザグ堰3を溢水して集水桶4に集めら
れ、導出口10から取出される。
On the other hand, the clarified water in the raw water from which suspended solids have been removed rises in the clarification chamber la due to the pushing force of the downstream flow, overflows the zigzag weir 3 formed on the outer periphery of the clarification chamber 1a, and is collected in the water collection trough 4. , taken out from the outlet 10.

〔発明の効果〕〔Effect of the invention〕

以上のように本発明の装置は渦巻き水路の中心部に、導
入原水を水平方向に方向づけろ水流偏向手段を設けであ
るので清澄室の原水に安定した流動エネルギーを付与す
ることができる。従って、原水中の懸濁成分を効率良く
沈澱、濃縮できる。
As described above, since the device of the present invention is provided with a water flow deflecting means for horizontally directing the introduced raw water in the center of the spiral waterway, it is possible to impart stable flow energy to the raw water in the clarification chamber. Therefore, suspended components in raw water can be efficiently precipitated and concentrated.

また、渦巻き水路仕切板の外側端縁は清澄室の内壁から
離し、その間に流路を形成しであるので清澄室内の原水
は緩やかに旋回し続け、滞留や逆流の生ずるおそれがな
い。従って、従来のように清澄水が下方の濃縮室の沈澱
物を巻き上げて再懸濁するおそれがなく、処理水は常に
所定の清澄度を保持して取出すことができる。
Further, since the outer edge of the spiral waterway partition plate is separated from the inner wall of the clarification chamber and a flow path is formed therebetween, the raw water in the clarification chamber continues to swirl gently, and there is no risk of stagnation or backflow. Therefore, there is no risk that the clear water will stir up and resuspend the precipitate in the concentration chamber below, unlike in the past, and the treated water can always be taken out while maintaining a predetermined level of clarity.

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

第1図は本発明装置の一実施例の側面図、第2図はその
平面図、第3図は第1図の縦断面図、第4図は第3図の
IV−[1/線断面図、第5図は別の実施例による第3
図相当図である。 1・−・沈澱槽、la・・・清澄室、1b・・・濃縮室
、2・・・スラッジ取出口、3・・・ジグザグ堰、4・
・・集水桶、5・・・禍巻き水路仕切板、7・・・支持
ブラケット、8・・・導入管、9・・・水流偏向手段、
9a・・・螺旋状底板、9b・・・導入口。
FIG. 1 is a side view of one embodiment of the device of the present invention, FIG. 2 is a plan view thereof, FIG. 3 is a vertical sectional view of FIG. 1, and FIG. 4 is a cross section taken along line IV-[1/ of FIG. FIG. 5 shows a third example according to another embodiment.
It is a figure equivalent figure. 1... Sedimentation tank, la... Clarification chamber, 1b... Concentration chamber, 2... Sludge outlet, 3... Zigzag weir, 4.
...Water collection bucket, 5...Water flow channel partition plate, 7...Support bracket, 8...Introduction pipe, 9...Water flow deflection means,
9a...Spiral bottom plate, 9b...Inlet.

Claims (1)

【特許請求の範囲】 (1)円筒条清澄室1aの下方に濃縮室1bを一体に連
通させてなる沈澱槽1と、この沈澱槽1の清澄室1aに
垂直に配置された一連の渦巻き状水路仕切板5と、水路
仕切板5の渦巻き中心部に挿入された懸濁原水導入管8
とを有する懸濁水の沈降浄化装置において、 渦巻き状水路仕切板5を、その外側端縁5′と清澄室1
a内壁の間に水路6を形成するように離隔させて配置す
るとともに、該仕切板5の渦巻き中心部に、清澄室1a
の導入原水を渦巻き状水路仕切板5に沿って押出すため
の水流偏向手段9を設けたことを特徴とする懸濁水沈降
浄化装置(2)水流偏向手段9が、渦巻き状水路仕切板
5の渦巻き中心部の水路下部に沿って配設した螺旋状の
底板9aからなることを特徴とする特許請求の範囲第1
項記載の懸濁水沈降浄化装置 (3)水流偏向手段9が、清澄室1a内の原水の重心レ
ベルにおいて原水導入管8の横方向に向けて設けた導入
口9bからなることを特徴とする特許請求の範囲第1項
記載の懸濁水沈降浄化装置
[Scope of Claims] (1) A sedimentation tank 1 formed by integrally communicating a concentration chamber 1b below a cylindrical clarification chamber 1a, and a series of spiral-shaped sedimentation tanks arranged perpendicularly to the clarification chamber 1a of this sedimentation tank 1. Waterway partition plate 5 and suspended raw water introduction pipe 8 inserted into the spiral center of waterway partition plate 5
In the apparatus for sedimentation and purification of suspended water having
The clarification chamber 1a is spaced apart from each other so as to form a water channel 6 between the inner walls of the partition plate 5.
Suspended water sedimentation purification device (2) characterized in that it is provided with a water flow deflection means 9 for pushing out the introduced raw water along the spiral waterway partition plate 5 (2) The water flow deflection means 9 is Claim 1, characterized in that it consists of a spiral bottom plate 9a disposed along the lower part of the water channel at the center of the spiral.
Suspended water sedimentation purification device (3) as described in 1. A patent characterized in that the water flow deflection means 9 is comprised of an inlet 9b provided laterally to the raw water inlet pipe 8 at the level of the center of gravity of the raw water in the clarification chamber 1a. Suspended water sedimentation purification device according to claim 1
JP10161686A 1986-05-01 1986-05-01 Apparatus for purifying suspension by sedimentation Pending JPS62258714A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10161686A JPS62258714A (en) 1986-05-01 1986-05-01 Apparatus for purifying suspension by sedimentation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10161686A JPS62258714A (en) 1986-05-01 1986-05-01 Apparatus for purifying suspension by sedimentation

Publications (1)

Publication Number Publication Date
JPS62258714A true JPS62258714A (en) 1987-11-11

Family

ID=14305337

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10161686A Pending JPS62258714A (en) 1986-05-01 1986-05-01 Apparatus for purifying suspension by sedimentation

Country Status (1)

Country Link
JP (1) JPS62258714A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0826405A1 (en) * 1996-08-30 1998-03-04 Lucas Industries Public Limited Company Sedimenter
JP2002542008A (en) * 1999-04-15 2002-12-10 ハイドロ インターナショナル ピーエルシー Hydrodynamic vortex separator
CN102805956A (en) * 2011-06-05 2012-12-05 赵峰 Vertical pipe type sludge-water separation treating device
CN105498943A (en) * 2015-12-16 2016-04-20 通辽矽砂工业公司 Steady flow multipurpose silicon sand pump pool

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4926855A (en) * 1972-07-06 1974-03-09

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4926855A (en) * 1972-07-06 1974-03-09

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0826405A1 (en) * 1996-08-30 1998-03-04 Lucas Industries Public Limited Company Sedimenter
US5900149A (en) * 1996-08-30 1999-05-04 Lucas Industries Public Limited Company Sedimenter
JP2002542008A (en) * 1999-04-15 2002-12-10 ハイドロ インターナショナル ピーエルシー Hydrodynamic vortex separator
CN102805956A (en) * 2011-06-05 2012-12-05 赵峰 Vertical pipe type sludge-water separation treating device
CN105498943A (en) * 2015-12-16 2016-04-20 通辽矽砂工业公司 Steady flow multipurpose silicon sand pump pool

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