JPH0220002Y2 - - Google Patents
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- Publication number
- JPH0220002Y2 JPH0220002Y2 JP1984144973U JP14497384U JPH0220002Y2 JP H0220002 Y2 JPH0220002 Y2 JP H0220002Y2 JP 1984144973 U JP1984144973 U JP 1984144973U JP 14497384 U JP14497384 U JP 14497384U JP H0220002 Y2 JPH0220002 Y2 JP H0220002Y2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- liquid
- inlet
- solid
- sewage
- 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
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Description
【考案の詳細な説明】
〔産業上の利用分野〕
本考案は、下水道施設における下水中の砂など
の如き液中の固形物を有効に分離する固液分離水
槽に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a solid-liquid separation tank that effectively separates solid matter in liquid such as sand in sewage in sewage facilities.
下水処理場における従来の沈砂池は、下水管か
ら流入してきた下水を長方形の極めて大きい水槽
へ導き、流速を著しく低下させて比重の大きい砂
などの固形物を底面へ沈降させ、底面に沈降、堆
積した固形物をレーキ等により機械的に掻き集め
て除去するものであつた。そのため、従来の沈砂
池は、極めて広大な設置面積が必要であり、また
堆積した砂等を掻き集め、除去する機械的設備が
必要であつた。
Conventional settling basins at sewage treatment plants guide the sewage flowing in from the sewage pipes into an extremely large rectangular water tank, which significantly reduces the flow velocity and allows solids such as sand with a high specific gravity to settle to the bottom. The accumulated solids were removed by mechanically scraping them with a rake or the like. Therefore, conventional sand settling basins require an extremely large installation area, and also require mechanical equipment to scrape up and remove accumulated sand and the like.
(考案が解決しようとする問題点)
このような欠点を改良するために、例えば、特
開昭59−109632に示す如き旋回流を利用した固液
分離装置が発明されているが、この場合、流入口
から入つた被処理液中の砂などの固液物の一部が
放流口から流出し、分離が不十分な場合があると
いう問題点を有するものであつた。(Problems to be solved by the invention) In order to improve such drawbacks, a solid-liquid separation device using swirling flow has been invented, for example, as shown in Japanese Patent Application Laid-open No. 59-109632, but in this case, This method has a problem in that a portion of the solid-liquid substances such as sand in the liquid to be treated that enters from the inlet flows out from the outlet, resulting in insufficient separation.
また、流入口より放流口が下方にある場合には
流入路の液が満管とならず自由表面を持ち、流入
速度の制御が困難となり、流速が大き過ぎて沈殿
を防げることがあつた。 Further, when the outlet is located below the inlet, the liquid in the inlet channel is not full and has a free surface, making it difficult to control the inflow velocity, and the flow velocity is sometimes too high to prevent precipitation.
また、固形物分離装置として実願昭57−20373
の如く、放流口を流入口より高い位置に設け、両
者の間にバツフルを設けたものが知られている
が、バツフルは小さな通孔を残すのみで槽の横断
面を殆どカバーして固形物の流出を阻止する隔壁
の作用をしており、固形物をこのバツフルより下
側の室にて沈殿せしめ、清浄化した上部の水を通
孔して上側の室に導き流出するようにしているの
で、下側の室はかなり大きなものとなり小型化す
ることは困難であつた。 Also, as a solid matter separator
It is known that the outlet is placed at a higher position than the inlet, and a buttful is provided between the two, but the buttful only leaves a small hole and covers most of the cross section of the tank, allowing solids to flow through the tank. Solids are allowed to precipitate in the chamber below this butthole, and the purified water from the upper part is passed through the hole and led to the upper chamber where it flows out. Therefore, the lower chamber was quite large and it was difficult to downsize it.
本考案は、このような問題点を解決し、比較的
小さい設置面積で多量の下水を分離効率よく処理
することのできる固液分離水槽を提供することを
目的とする。 An object of the present invention is to solve these problems and provide a solid-liquid separation tank that can separate and efficiently treat a large amount of sewage with a relatively small installation area.
本考案は、ほぼ円形の側壁と、底面とを有し、
中に収容した被処理液を旋回せしめながら固液分
離を行う固液分離水槽において、被処理液の流入
路を前記側壁に接線方向に接続して備え、該流入
路の末端の流入口の少なくとも上縁幅にわたつ
て、該流入口の上縁か、またはそれより高い位置
で槽内に延設される分離板を設け、該分離板の上
方で、前記流入口近傍に処理済液を槽外に導く放
流口を開口設備したことを特徴とする固液分離水
槽である。
The present invention has a substantially circular side wall and a bottom surface,
A solid-liquid separation water tank in which solid-liquid separation is performed while swirling a liquid to be treated stored therein, is provided with an inflow path for the liquid to be treated tangentially connected to the side wall, and at least one of the inflow ports at the end of the inflow path is provided. A separation plate extending into the tank at or higher than the upper edge of the inlet is provided over the width of the upper edge, and the treated liquid is placed in the tank above the separation plate and near the inlet. This is a solid-liquid separation water tank characterized by having an open outlet that leads to the outside.
本考案は上記のように構成されており、槽内の
主な流れとして流入口から放流口までの間に円滑
な上昇旋回流が形成される。
The present invention is configured as described above, and a smooth upward swirling flow is formed as the main flow in the tank from the inlet to the outlet.
しかして、流入口から流入した原水は分離板の
下側を案内されて槽内に入り、放流口に近付く浄
水は、分離板の上側を案内されながら水平な旋回
流とし近付き放流口に吸い込まれる。 The raw water that flows in from the inlet is guided under the separation plate and enters the tank, and the purified water that approaches the outlet becomes a horizontal swirling flow while being guided above the separation plate and is sucked into the outlet. .
このとき、流入口から流入する原水と、分離板
の上で放流口に導かれる浄水とは分離板により積
極的に分離されるので、原水が直接放流された
り、折曲浄化度が高まつた水に浄化度の低い水が
混入して浄化度を再び低下せしめたりすることが
防がれ、短い流路(らせん状の上昇旋回流路)に
て高い分離効率を得ることができ、従つて小型の
装置で多量の下水を分離効率よく処理することが
できる。 At this time, the raw water flowing in from the inlet and the purified water guided to the outlet on the separation plate are actively separated by the separation plate, so the raw water is not directly discharged or the degree of purification is increased by bending. This prevents water with a low degree of purification from being mixed into the water and lowering the degree of purification again, and high separation efficiency can be obtained with a short channel (spiral upward swirling channel). A large amount of sewage can be separated and treated efficiently with a small device.
なお、下水を水槽内で旋回させるとき、旋回流
に対して直角な面内において「二次流れ」が生ず
ることが知られている。この二次流れは、旋回流
の上部では水槽の外壁に向かい、旋回流の下部に
おいては壁と反対に水槽の中心方向に向かつて流
れるものである。そのため、水槽の底面に堆積し
た砂などの固形物は中心に向かつて押しやられる
傾向が生ずるので、槽底の沈殿物が効果的に中央
に収集され、これをポンプなどで排出することが
好適である。 It is known that when sewage is swirled in a water tank, a "secondary flow" occurs in a plane perpendicular to the swirling flow. This secondary flow flows toward the outer wall of the tank in the upper part of the swirling flow, and flows toward the center of the tank in the opposite direction to the wall in the lower part of the swirling flow. Therefore, solid matter such as sand that has accumulated on the bottom of the aquarium tends to be pushed toward the center, so it is preferable to effectively collect the sediment at the bottom of the tank in the center and drain it using a pump or the like. be.
本考案の実施例を図面を用いて説明する。 Embodiments of the present invention will be described with reference to the drawings.
第1図a及びbにおいて、固液分離水槽1は、
ほぼ円形(円形、楕円形、長円形などの類似円形
或いはスパイラル状)の側壁2及び底面3を有し
ている。この水槽1には被処理液例えば下水を側
壁2に対して接線方向に導入して水槽1内におけ
る液に旋回運動を与えるよう末端が流入口5で開
口する流入路4を側壁2接線方向に設ける。流入
口5の位置は、一部が底面3にかかつてもよく、
又、底面3のみにあつもよい。底面3は外周から
中心に向かつて傾斜している。底面3は水平に形
成してよいが沈殿性の固形物を底部中心に集積す
るためには傾斜している方が効果的である。 In FIGS. 1a and 1b, the solid-liquid separation tank 1 is
It has a side wall 2 and a bottom surface 3 that are approximately circular (circular, oval, oval, similar circular shape, or spiral shape). In this water tank 1, an inflow channel 4 whose end opens at an inlet 5 is provided in a tangential direction to the side wall 2 to introduce a liquid to be treated, such as sewage, in a tangential direction to the side wall 2 and give a swirling motion to the liquid in the tank 1. establish. The position of the inflow port 5 may be such that a part thereof is on the bottom surface 3.
Alternatively, it may be placed only on the bottom surface 3. The bottom surface 3 is inclined from the outer periphery toward the center. The bottom surface 3 may be formed horizontally, but it is more effective to have it sloped in order to collect the precipitable solids in the center of the bottom surface.
水槽1の底面3の中央付近の沈砂受3aには分
離した固形物を多く含む濃縮液を槽外に導く濃縮
液排出部としてポンプ6aを有する排出管6が上
方から挿入され開口し、被処理液に含まれている
沈殿性の固形物を、旋回流及び二次流により底部
に集積せしめて被処理液と共に濃縮液として槽外
に排出するものである。 A discharge pipe 6 having a pump 6a is inserted from above into the sediment receiver 3a near the center of the bottom surface 3 of the water tank 1 to serve as a concentrate discharge section for guiding the concentrated liquid containing a large amount of separated solids to the outside of the tank. Precipitable solids contained in the liquid are accumulated at the bottom by swirling flow and secondary flow, and are discharged out of the tank as a concentrated liquid together with the liquid to be treated.
水槽1の側壁2には放流口9が設けられてい
る。この放流口9は、流入口5から側壁2の周上
に旋回流の流れの向きに沿つて少し下流側に外れ
た位置で、180゜までの間の位置に設けるのが好ま
しい。また、その高さは流入口5より高い位置と
する。そして流入口5と放流口9の高さの中間
に、かつ旋回流流れの向きに沿つて流入口5から
放流口9までの範囲にわたつて、ほぼ水平な分離
板10が設けられている。即ち、分離板10は流
入口5の上縁幅よりも大きな幅にわたつて流入口
の上縁か又はそれより高い位置(本実施例ではや
や高い位置)で水槽1内に延設され、分離板10
の上方で流入口5近傍に放流口9が開口配備され
ている。 A water outlet 9 is provided in the side wall 2 of the water tank 1. The discharge port 9 is preferably provided at a position slightly downstream of the inlet 5 on the circumference of the side wall 2 along the flow direction of the swirling flow, and at a position of up to 180°. Further, its height is set higher than the inlet 5. A substantially horizontal separation plate 10 is provided midway between the heights of the inlet 5 and the outlet 9 and extending along the direction of the swirling flow from the inlet 5 to the outlet 9. That is, the separation plate 10 is extended into the water tank 1 over a width larger than the upper edge width of the inlet 5 at a position higher than the upper edge of the inlet (in this embodiment, a slightly higher position), and is separated. Board 10
An outlet 9 is provided above the inlet 5 near the inlet 5 .
砂などの固形物を混入した下水は、流入路4を
経て流入口5から水槽1内に流入し、側壁2に沿
つて矢印のように旋回する。流れの旋回と共に、
下水中の砂などは底面3へ沈降する。旋回流に対
しては、前述のように、二次流れ7が生じる。こ
の底面中心に向かう二次流れ7と底面3の傾斜と
によつて、沈降した沈砂8は中心に向けて押しや
られ、沈砂受3aに集められる。沈砂受3aの砂
の量が一定量以上になると、ポンプ6aを作動し
て沈殿した砂などの固形物を含む濃縮度を排出管
6により吸い上げ、外部に排出する。 Sewage mixed with solids such as sand flows into the water tank 1 from the inlet 5 via the inlet channel 4, and swirls along the side wall 2 as shown by the arrow. With the swirl of the flow,
Sand and the like in the sewage settles to the bottom surface 3. For swirling flows, secondary flows 7 occur, as described above. Due to the secondary flow 7 directed toward the center of the bottom surface and the slope of the bottom surface 3, the settled sand 8 is pushed toward the center and collected in the sand receptacle 3a. When the amount of sand in the sand receiver 3a reaches a certain level or more, the pump 6a is operated to suck up the concentrated content including solid matter such as precipitated sand through the discharge pipe 6 and discharge it to the outside.
浄化されつつある下水の主な流れは上昇旋回し
ながららせん運動を行つて分離板10の上を通つ
て、放流口9に向かつて案内される。放流口9は
流入口5の真上付近或いはその近傍にあるので、
下水は水槽1内をほぼ360゜或いはそれ以上流れる
ことになり、十分に砂などの固形物を分離するこ
とができる。 The main flow of the sewage being purified is guided in a spiral upward spiral movement past the separator plate 10 towards the outlet 9. Since the outlet 9 is located directly above or in the vicinity of the inlet 5,
The sewage flows through approximately 360 degrees or more within the water tank 1, and solid matter such as sand can be sufficiently separated.
また分離板10の分離作用により流入してくる
下水と浄化された下水との混合が生ずることがな
く、又流入してくる下水が砂などを分離しないう
ちに直線放流口9に素通り状態で流入することも
ない。 In addition, due to the separation action of the separation plate 10, inflowing sewage and purified sewage do not mix, and the inflowing sewage flows directly into the straight outlet 9 without separating sand, etc. There's nothing to do.
さらに、放流口9は流入口5よりも上方にある
ので、流入路4の中には下水が充満して自由表面
を生ずることはない。従つて流入速度が制御し易
く、流れの乱れも小さいので、砂などの沈降が妨
げられることもない。 Furthermore, since the outlet 9 is located above the inlet 5, the inlet channel 4 will not be filled with sewage and create a free surface. Therefore, since the inflow speed is easily controlled and the turbulence of the flow is small, the settling of sand etc. is not hindered.
次に第2図a,bにおいて、固液分離水槽1は
第1図a,bに示すものと同様にほぼ円形の側壁
2と、中心に向かつて傾斜した底面3とを有し、
底面の中央部付近に設けられた沈砂受3aにポン
プ6aを備えた排出管6が挿入されている。 Next, in FIGS. 2a and 2b, the solid-liquid separation tank 1 has a substantially circular side wall 2 and a bottom surface 3 that slopes toward the center, similar to that shown in FIGS. 1a and 1b.
A discharge pipe 6 equipped with a pump 6a is inserted into a sediment receptacle 3a provided near the center of the bottom surface.
しかして、側壁2に対し接線方向に設けられた
流入路4は水槽1の内部にまで突入し、その末端
の流入口5が槽内に開口している。そしてその
際、流入路4の上壁が分離板10を兼用してい
る。下水の流れは第1図a,bの場合と同様であ
る。 Thus, the inflow channel 4 provided tangentially to the side wall 2 extends into the interior of the water tank 1, and the inflow port 5 at its end opens into the tank. In this case, the upper wall of the inflow path 4 also serves as the separation plate 10. The flow of sewage is the same as in Figures 1a and b.
本考案は、上記のように構成されているので、
流入水が槽内を少なくともほぼ360度旋回移動す
る間に分離が充分行われるばかりでなく、原水が
直接放流されたり、折曲浄化度が高まつた水に浄
化度の低い水が混入して浄化度を再び低下せしめ
たりすることが防がれ、短い流路(らせん状の上
昇旋回流路)にて高い分離効率を得ることがで
き、従つて小型の装置で多量の下水を分離効率よ
く処理することができ、また、安定した二次流れ
が形成され槽底の沈殿物が効果的に中央に収集さ
れ、排出が容易となり、実用上極めて大なる効果
を奏する。
Since the present invention is configured as described above,
Not only is sufficient separation carried out while the inflow water rotates at least approximately 360 degrees within the tank, but it also prevents raw water from being directly discharged, or contaminating water with a higher degree of purification with water of a lower degree of purification. This prevents the degree of purification from decreasing again, and allows high separation efficiency to be achieved with a short flow path (spiral ascending swirl flow path). Therefore, a large amount of sewage can be separated efficiently with a small device. In addition, a stable secondary flow is formed, and the sediment at the bottom of the tank is effectively collected in the center, making it easy to discharge, which is extremely effective in practice.
第1図a,bは本考案の実施例の平面図及び断
面側面図、第2図a,bは他の実施例の平面図及
び断面側面図である。
1……水槽、2……側壁、3……底面、3a…
…沈砂受、4……流入路、5……流入口、6……
排出管、6a……ポンプ、7……二次流れ、8…
…沈砂、9……放流口、10……分離板。
1A and 1B are a plan view and a sectional side view of an embodiment of the present invention, and FIGS. 2A and 2B are a plan view and a sectional side view of another embodiment. 1...Aquarium, 2...Side wall, 3...Bottom surface, 3a...
...Sand receptacle, 4...Inflow channel, 5...Inlet, 6...
Discharge pipe, 6a... pump, 7... secondary flow, 8...
...Sand, 9... Outlet, 10... Separation plate.
Claims (1)
た被処理液を旋回せしめながら固液分離を行う固
液分離水槽において、被処理液の流入路を前記側
壁に接線方向に接続して備え、該流入路の末端の
流入口の少なくとも上縁幅にわたつて、該流入口
の上縁か、またはそれより高い位置で槽内に延設
される分離板を設け、該分離板の上方で、前記流
入口近傍に処理済液を槽外に導く放流口を開口配
備したことを特徴とする固液分離水槽。 In a solid-liquid separation water tank that has a substantially circular side wall and a bottom surface and performs solid-liquid separation while swirling a liquid to be treated contained therein, an inflow path for the liquid to be treated is connected tangentially to the side wall. a separation plate extending into the tank at or higher than the upper edge of the inflow port over at least the width of the upper edge of the inflow port at the end of the inflow passage; A solid-liquid separation tank, characterized in that a discharge port for guiding the treated liquid out of the tank is provided near the inlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1984144973U JPH0220002Y2 (en) | 1984-09-27 | 1984-09-27 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1984144973U JPH0220002Y2 (en) | 1984-09-27 | 1984-09-27 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6161002U JPS6161002U (en) | 1986-04-24 |
| JPH0220002Y2 true JPH0220002Y2 (en) | 1990-06-01 |
Family
ID=30703232
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1984144973U Expired JPH0220002Y2 (en) | 1984-09-27 | 1984-09-27 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0220002Y2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5720373A (en) * | 1980-07-14 | 1982-02-02 | Hitachi Ltd | Heat-sensitive recording head and production thereof |
-
1984
- 1984-09-27 JP JP1984144973U patent/JPH0220002Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6161002U (en) | 1986-04-24 |
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