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JPH0143589B2 - - Google Patents
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JPH0143589B2 - - Google Patents

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Publication number
JPH0143589B2
JPH0143589B2 JP19188782A JP19188782A JPH0143589B2 JP H0143589 B2 JPH0143589 B2 JP H0143589B2 JP 19188782 A JP19188782 A JP 19188782A JP 19188782 A JP19188782 A JP 19188782A JP H0143589 B2 JPH0143589 B2 JP H0143589B2
Authority
JP
Japan
Prior art keywords
water
tank
side wall
flow
solids
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
Application number
JP19188782A
Other languages
Japanese (ja)
Other versions
JPS5982988A (en
Inventor
Koichi Yamanaka
Tetsuo Goto
Masanori Aoki
Isao Kataoka
Toshiaki Nishiwaki
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP19188782A priority Critical patent/JPS5982988A/en
Priority to US06/538,992 priority patent/US4517091A/en
Publication of JPS5982988A publication Critical patent/JPS5982988A/en
Publication of JPH0143589B2 publication Critical patent/JPH0143589B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、下水などの如く、固形物を含んでい
る各種廃水などの被処理水の固液分離を行う固液
分離装置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 separator that performs solid-liquid separation of water to be treated, such as various types of wastewater containing solids, such as sewage. .

〔従来の技術〕[Conventional technology]

一般に、合流式下水道から雨天時に未処理で放
流される雨天時越流水は公共水面の水質汚濁源と
して重要な問題を提起している。
In general, overflow water discharged untreated from combined sewer systems during rainy days poses important problems as a source of water pollution in public waters.

この越流水質を改善するために、用いられる合
流式下水越流調整装置は2つの働き(量と質の制
御)を強めるような下水道システムが必要とな
る。即ち、下水中の固形物を濃縮して遮集管(下
水処理場)へ送ることと雨天時の過剰な下水を放
流口に分流することである。
In order to improve the quality of this overflow water, the combined sewage overflow control device used requires a sewerage system that strengthens two functions (control of quantity and quality). That is, solid matter in sewage is concentrated and sent to an interceptor pipe (sewage treatment plant), and excess sewage on rainy days is diverted to an outlet.

この越流調整装置に用いる固液分離装置として
従来用いられているものに、いわゆるスワール分
水槽が知られている。例えば、スワール分水槽の
一例を第1図及び第2図に示せば、1は円筒形の
スワール分水槽の外殻、2は分水槽の下部に位置
して流入下水或いは汚濁物質を含む廃水を接線の
方向の向きに槽内に導入する流入渠、3は流入下
水を槽の周辺部の長い距離をとつて施回させるた
めの流向制御板、4は処理水を排出するために槽
の底部に垂直に設けられた管(ダウンシヤフト)、
5はダウンシヤフト4の頂部に取付けられた集水
盆、6は集水盆5の周縁に取付けられた越流堰、
7は越流堰6の外周を囲んでこれと間隔をおいて
設けられた、水面に浮上するスカムをさえぎるた
めのスカムリングである。
A so-called swirl water diversion tank is known as a conventional solid-liquid separation device used in this overflow adjustment device. For example, an example of a swirl water tank is shown in Figures 1 and 2, where 1 is a cylindrical outer shell of the swirl water tank, and 2 is located at the bottom of the water tank to collect inflowing sewage or wastewater containing pollutants. An inflow conduit that is introduced into the tank in the tangential direction; 3 is a flow direction control plate for distributing inflow sewage over a long distance around the periphery of the tank; 4 is a bottom of the tank for discharging treated water; A pipe installed perpendicular to (downshaft),
5 is a water collection basin attached to the top of the downshaft 4; 6 is an overflow weir attached to the periphery of the water collection basin 5;
Reference numeral 7 denotes a scum ring that surrounds the outer periphery of the overflow weir 6 and is provided at a distance therefrom to block scum floating on the water surface.

8はスポイラーで、集水盆5にスカムリング7
を連結し、集水盆上及びスカムリングと越流堰間
の水の回転エネルギーを減少させてダウンシヤフ
トの容量を増し、固液分離効率を高めるものであ
る。9は水面浮上性物質を捕集し、これを集水盆
5の下へ導くためのスカムトラツプ、10は汚水
排水管、11は晴天時に固形物の堆積するのを防
止するために流入渠2と汚水排出管10とを結び
つけて、槽の床上に設けられた導溝で、12は処
理水排出管である。
8 is a spoiler, scum ring 7 is in water collection basin 5
This system reduces the rotational energy of water above the water collection basin and between the scum ring and overflow weir, increasing the capacity of the downshaft and increasing solid-liquid separation efficiency. Reference numeral 9 indicates a scum trap for collecting substances floating on the water surface and guiding them to the bottom of the water collection basin 5; 10 indicates a sewage drain pipe; and 11 indicates an inlet drain 2 to prevent solids from accumulating on sunny days. A guide groove is provided on the floor of the tank to connect the sewage discharge pipe 10, and 12 is a treated water discharge pipe.

上記構造のスワール分水槽による流入下水(或
いは廃水)の処理は以下の如く行われる。流入下
水はスワール分水槽の下部に設けられた流入渠2
から槽内に接線方向に導入され、流向制御板3に
よつてダウンシヤフト4を中心に施回させられな
がら槽内を上昇し、その間に下水中の沈砂分或い
は沈殿性浮遊物は重力と慣性力によつて沈降して
槽の中央部に集められ、汚水排出管10を経て排
出される。沈殿性浮遊物を除去された下水は、そ
の水面浮上性物質をスカムリング7でさえぎられ
て除去され、清澄水はスカムリング7の下縁をく
ぐりぬけて越流堰6の上縁を超えて集水盆5に集
まり、スポイラー8により回転エネルギーを減少
させられ、ダウンシヤフト4を通じて、処理水と
し処理水排出管12から排出される。
Treatment of inflowing sewage (or wastewater) by the swirl water diversion tank having the above structure is performed as follows. Inflow sewage flows into inflow drain 2 installed at the bottom of the swirl diversion tank.
The sewage is introduced into the tank in a tangential direction and ascends through the tank while being rotated around the downshaft 4 by the flow direction control plate 3. During this time, the sediment or sedimentary suspended matter in the sewage is absorbed by gravity and inertia. It settles under the force and is collected in the center of the tank, and is discharged through the sewage discharge pipe 10. The sewage from which sedimentary floating substances have been removed is removed by blocking the substances that float on the water surface with the scum ring 7, and the clear water passes through the lower edge of the scum ring 7 and collects over the upper edge of the overflow weir 6. The water collects in the water basin 5, has its rotational energy reduced by the spoiler 8, and is discharged through the downshaft 4 as treated water from the treated water discharge pipe 12.

前記スカムリング7でさえぎられた水面浮上性
物質は、スカムリング周囲を浮遊してスカムトラ
ツプ9で捕集され、水流によつて集水盆5の下に
引きこまれ、越流堰6が集水盆の下方にのびてい
る部分の内側に貯留される。この水面浮上性物質
は槽内の水位が低下すると槽中央部に集まり汚水
排出管10から排出される。
The substances that float on the water surface that are intercepted by the scum ring 7 float around the scum ring, are collected by the scum trap 9, and are drawn under the water collection basin 5 by the water flow, and the overflow weir 6 collects the water. It is stored inside the downwardly extending part of the tray. When the water level in the tank decreases, these substances that float on the water surface gather in the center of the tank and are discharged from the wastewater discharge pipe 10.

このようなスワール分水槽を用いる下水処理に
おいては、晴天時の低量時には全ての流入下水が
案内溝に沿つて直接汚水管へと導かれ下水処理場
に運ばれる。雨天時の流入量が多くなり水槽内の
水位が高くなつた時には、前述のように固形物を
分離する。多くの固形物を含んだ高濃度の汚水量
は濃縮の結果量は少なくなり、オリフイスから汚
水管へ送られる。他方残りの清澄な下水は量が多
く越流堰を超えていく。放流先の水質基準によつ
てこの越流水はさらに処理されるかあるいは放流
されることになる。
In sewage treatment using such a swirl diversion tank, when the amount of sewage is low on sunny days, all inflowing sewage is guided directly to the wastewater pipe along the guide groove and transported to the sewage treatment plant. When it rains and the water level in the tank becomes high due to the large amount of inflow, the solids are separated as described above. The amount of highly concentrated sewage containing many solids is reduced as a result of concentration and is sent to the sewage pipe from the orifice. On the other hand, the remaining clear sewage is large in volume and flows over the overflow weir. Depending on the water quality standards at the destination, this overflow water may be further treated or released.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

ところが、このスワール分水槽は次の如き欠点
を有する。
However, this swirl water tank has the following drawbacks.

比重が1より小さい浮上物の分離率が悪い。
比重が1よりも小さい浮遊性の固形物(通称S.
S)については分離機能は持つているが水槽の
水位が低下しないと排出機能が作用しないため
に貯留能力に限界がある。そのためにこれを超
えた場合、放流(越流)水中に浮遊物が混じつ
て流出し結果として分離性能が低下している。
水槽の水位が上昇して越流する状況にある場
合、スカムリング7の下端から越流堰6に流入
する流速が速くなり、この速い流れに浮上性固
形物が同伴されて処理水排出管12に流出する
ために分離効率が低下する。流速の速くなる原
因は、流入量が汚水排出管10から流出する量
より大幅に増加したときに水位が上昇して越流
する水量であるから水量としては大きいものと
なるためである。即ち、越流水はスカムリング
の下端から集水盆の上を流れてダウンシヤフト
に流入するが、この量が多いために流速が早く
水中に浮遊している固形物は、この越流水に同
伴されてダウンシヤフトに流入して分離率を下
げている。集水盆の下側には初期に流入する浮
遊性の固形物は集積されるが水位が上つて越流
堰から水が流れ初めると浮遊性の固形物を分離
する能力は著しく低下する。
Separation rate of floating objects with specific gravity less than 1 is poor.
Floating solids with specific gravity less than 1 (commonly known as S.
Regarding S), it has a separation function, but its storage capacity is limited because the discharge function does not work unless the water level in the tank decreases. Therefore, when this value is exceeded, suspended matter is mixed with the discharged (overflow) water and flows out, resulting in a decrease in separation performance.
When the water level in the water tank rises and the water overflows, the flow velocity flowing into the overflow weir 6 from the lower end of the scum ring 7 increases, and floating solids are entrained in this fast flow, and the treated water discharge pipe 12 Separation efficiency decreases due to outflow. The reason why the flow rate increases is that when the inflow amount increases significantly compared to the outflow amount from the wastewater discharge pipe 10, the water level rises and the amount of water overflows, resulting in a large amount of water. In other words, the overflow water flows from the lower end of the scum ring over the water collection basin and into the downshaft, but due to the large amount of water, the flow rate is fast and the solids suspended in the water are entrained in the overflow water. and flows into the downshaft, reducing the separation rate. Floating solids that initially flow into the basin are accumulated at the bottom of the catchment basin, but when the water level rises and water begins to flow from the overflow weir, the ability to separate floating solids decreases significantly.

浮上物の分離排出を常時行うことができな
い。例えば降雨時に常時行うことができない。
It is not possible to separate and discharge floating objects all the time. For example, it cannot be carried out all the time when it is raining.

スワール型分水槽では、分離した浮上性固形
物を集水盆の下部に貯留するだけで、水位が低
下するまでは水槽の外部へ排出する機能を持つ
ていない。なんとならば、この固形物は水に浮
かんでおり、槽の底部に設けた汚水排出管と集
積した固形物の下層との間にある水の層でさえ
ぎられているためである。そのため水位が上昇
してから流入する下水に含まれている浮上性固
形物はスカムトラツプ9で捕集されるよりもス
カムリングの下端から越流堰を越えて流れる流
れ(流速が早いので)に同伴される量の方が多
くなる。
Swirl-type water tanks simply store separated floating solids in the lower part of the water collection basin, and do not have the function of discharging them to the outside of the tank until the water level drops. This is because the solids are floating in the water and are blocked by a layer of water between the sewage discharge pipe installed at the bottom of the tank and the lower layer of accumulated solids. Therefore, floating solids contained in the inflowing sewage after the water level rises are not collected by the scum trap 9, but are entrained by the flow flowing from the lower end of the scum ring over the overflow weir (because the flow velocity is faster). The amount received will be greater.

沈殿物の排出が困難である。 It is difficult to drain the sediment.

浮上性固形物を捕集するスカムトラツプやス
カムリングを設けているために槽内の二次流れ
の発達を阻害する。特に槽内で発生する二次流
れは、スカムリングの直径の投影円筒部と外周
壁との狭い間で生じているため勢いも弱く沈殿
物を水槽中心部に集積する力は弱い。そのため
に比重の大きな固形物は底面に沈降したその位
置にとどまり汚水排出管の開口部まで移動する
ことは少ない。従つて晴天時に堆積物を人手で
排除するなどの保守が必要となる。
A scum trap or scum ring is installed to collect floating solids, which inhibits the development of secondary flow within the tank. In particular, the secondary flow generated within the tank is generated in a narrow space between the projected cylindrical portion of the diameter of the scum ring and the outer circumferential wall, so its momentum is weak and the force of accumulating sediment in the center of the tank is weak. For this reason, solids with a high specific gravity remain in the position settled on the bottom surface and are unlikely to move to the opening of the wastewater discharge pipe. Therefore, maintenance such as manually removing deposits is required on sunny days.

固形物がつまり易い。 Solids can easily clog.

スワール型ではスカムリング、スカムトラツ
プなどを設けているために大きな固形物がこれ
らにからまつてつまる可能性がある。
Since the swirl type is equipped with scum rings, scum traps, etc., there is a possibility that large solids may become entangled in these.

本発明は、従来のもののこれらの欠点を除き、
浮上物を水面中心に集めて有効に排出することが
できる固液分離装置を提供することを目的とする
ものである。
The present invention eliminates these drawbacks of the conventional ones,
It is an object of the present invention to provide a solid-liquid separator that can collect floating objects at the center of the water surface and effectively discharge them.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は、側壁と底壁とで水平断面が円形状に
構成した槽に、前記側壁に対して接線方向に被処
理水を流入せしめる流入口を設けると共に、槽中
央部に直立して上端が開放され、かつ下端が前記
底壁を貫通している浮上物オーバーフロー管と、
前記側壁又は底壁の一部から分離後の被処理水を
排水せしめる排水部とを配備したことを特徴とす
る固液分離装置である。
The present invention provides a tank having a circular horizontal cross section with a side wall and a bottom wall, and an inlet for allowing water to be treated to flow in in a tangential direction to the side wall. a floating object overflow pipe that is open and whose lower end passes through the bottom wall;
The solid-liquid separator is characterized in that a drainage section is provided from a part of the side wall or the bottom wall to drain the separated water to be treated.

本発明は、施回流に伴う二次流れの作用をたく
みに利用して浮上物をオーバーフロー管の上端に
集中せしめて有効に排除するものである。
The present invention makes effective use of the effect of the secondary flow associated with the circulation flow to concentrate the floating objects at the upper end of the overflow pipe, thereby effectively eliminating them.

〔作用〕[Effect]

二次流れにつき説明すれば、水平断面が円形状
の水槽の接線方向から流入した流体は水槽内で回
転運動をする。これが水槽内の主流(一次流)と
なる。この流れは表面摩擦の影響によつて水面付
近の流体は水槽底面付近の流体より速く流れるた
め強い遠心力を受ける。また一定深さの流体中で
の圧力は外側で高く中心付近では低くなる。底面
付近における流体は底板の表面摩擦の影響によつ
て周方向の速度が小さいため遠心力は小さくなる
が水流により圧力勾配は他の部分と同様であるか
ら力のつり合いが破れて中心に向かう流れが生じ
ることになる。この流れが二次流れであり、中心
で合流して垂直上昇し、水面では放射状に流れて
外縁に達し、側壁に沿つて下降し循環する二次流
れとなる。
To explain the secondary flow, fluid that flows in from the tangential direction of a water tank having a circular horizontal cross section rotates within the water tank. This becomes the mainstream (primary flow) in the aquarium. Due to the effect of surface friction, this flow causes the fluid near the water surface to flow faster than the fluid near the bottom of the tank, so it is subject to a strong centrifugal force. Moreover, the pressure in a fluid at a certain depth is high on the outside and low near the center. The fluid near the bottom has a small circumferential velocity due to the surface friction of the bottom plate, so the centrifugal force is small, but the pressure gradient is the same as in other parts due to the water flow, so the balance of forces is broken and the flow moves toward the center. will occur. This flow is a secondary flow, which merges at the center and rises vertically, flows radially at the water surface, reaches the outer edge, and descends along the side wall to become a circulating secondary flow.

〔実施例〕〔Example〕

本発明の実施例につき概要を説明すれば、水槽
側面の上下方向の中心部ないし、底部に流入口を
設け流入水を接線方向に導入し、水が施回する力
を利用して沈殿性の固形物を沈殿させるととも
に、オーバーフロー管のほぼ全周にわたつて、水
槽側壁の上方から下方に向かつて下降し底面外周
から中心に向かつて流れる二流れを発生させ、こ
れによつて沈殿性固形物の沈降を促進し沈殿物を
外周から中心部に移動させる。
To give an overview of the embodiments of the present invention, an inlet is provided at the vertical center of the side surface of the aquarium or at the bottom, and the inflow water is introduced tangentially, and the force of the water is used to prevent sedimentation. In addition to precipitating the solids, two flows are generated over almost the entire circumference of the overflow pipe, from the top to the bottom of the side wall of the water tank and then downward, and then from the outer periphery of the bottom to the center, thereby removing the precipitable solids. promotes sedimentation and moves the precipitate from the periphery to the center.

また浮遊性物質は水中を施回しながら上昇し、
この二次流れによつて水面までの浮上を早くする
ようにした。
In addition, floating substances rise while circulating in the water,
This secondary flow allows for faster surfacing to the water surface.

ここでは、水槽の内部にはリングやスポイラ等
を設けずに中心部にオーバーフロー管だけを鉛直
に設けているために二次流れが強く発生してい
る。オーバーフロー管の側面に沿つて底部から表
面に向かう強い二次流れ現象が生じて、これによ
つて水中に浮遊する固形物はオーバーフロー管の
外周に沿つて水面まで浮上し、集積されオーバー
フロー管の開口部に流入する水流によつてオーバ
ーフロー管に捕集される。
Here, a strong secondary flow occurs because only an overflow pipe is provided vertically in the center without any ring or spoiler inside the water tank. A strong secondary flow phenomenon occurs along the sides of the overflow pipe from the bottom to the surface, which causes the solids suspended in the water to float up to the water surface along the outer circumference of the overflow pipe, where they are accumulated and dislodged from the opening of the overflow pipe. The water is collected in the overflow pipe by the water flowing into the section.

更に二次流れを強くするためには、水槽底面を
外周から中心部に向かつて中心が低くなるように
傾斜をつけると良い。
In order to further strengthen the secondary flow, it is best to slope the bottom of the tank from the outer periphery toward the center so that the center is lower.

本発明の実施例を第3図、第4図にて説明すれ
ば、水槽は水平断面が円形状の側壁13と底壁1
6とで構成されている。側壁13には下水の流入
筒14を設ける。この流入筒14の形状は断面円
形でも方形でもよいが、水槽内に水を側壁13に
対して接線方向に導入するようにして側壁13に
沿つて施回流が起きやすいようにする。オーバー
フロー管15は水槽の中央部に直立して設けて上
端が開放され下端は底壁16を貫通して設けら
れ、水の表面に浮上した固形物を水と一緒に水槽
の底部から排出するものである。オーバーフロー
管15の径により排出する水量が変わり、また二
次流れの強さにも影響を与える。オーバーフロー
管15の高さは、水槽の処理容量,分離効率に影
響する。オーバーフロー管15から排出する水量
を調整するために管の内部にオリフイスを設けて
もよい。
An embodiment of the present invention will be described with reference to FIGS. 3 and 4. The water tank has a side wall 13 and a bottom wall 1 having a circular horizontal cross section.
It consists of 6. A sewage inlet tube 14 is provided on the side wall 13. The shape of the inlet pipe 14 may be circular or rectangular in cross section, but water is introduced into the water tank in a tangential direction to the side wall 13 so that a circulating flow is likely to occur along the side wall 13. The overflow pipe 15 is installed upright in the center of the aquarium, has an open upper end, and a lower end that penetrates the bottom wall 16 to discharge solid matter floating on the surface of the water from the bottom of the aquarium together with the water. It is. The amount of water to be discharged changes depending on the diameter of the overflow pipe 15, which also affects the strength of the secondary flow. The height of the overflow pipe 15 affects the treatment capacity and separation efficiency of the water tank. An orifice may be provided inside the overflow pipe 15 to adjust the amount of water discharged from the pipe.

前記底壁16は平板で水平に配備してもよい
が、第4図のようにテーパー状に傾斜させた場合
二次流れが強くなり、分離効率を高めると共に底
部に沈殿する固形物を水槽中央部に集める力が強
くなる。底部排出管17は底壁16の中央近辺に
設けて下水中の比重が1よりも大きい固形物が底
部に沈殿堆積するがこれを水と一緒に水槽外に排
出するようにしてある。該底部排出管17の開口
部は底板上のオーバーフロー管15の周囲にでき
るだけ接近して設ける。この開口部の径はできる
だけ小さくした方が排出する水量を少なくする上
で好ましいが、大きな固形物によつて閉塞するこ
とも考えなければならない。この底部排出管17
は単数でなく複数設けてもよく、また、オーバー
フロー管15の底部周囲に設けてもよい。
The bottom wall 16 may be a flat plate and placed horizontally, but if it is tapered as shown in Figure 4, the secondary flow will become stronger, increasing the separation efficiency and directing the solids that settle at the bottom to the center of the tank. The ability to gather people in a club becomes stronger. The bottom discharge pipe 17 is provided near the center of the bottom wall 16 to discharge solid matter having a specific gravity greater than 1 in the sewage, which settles and accumulates at the bottom, out of the tank together with the water. The opening of the bottom discharge pipe 17 is provided as close as possible to the periphery of the overflow pipe 15 on the bottom plate. It is preferable to make the diameter of this opening as small as possible in order to reduce the amount of water to be discharged, but it must also be considered that it may be blocked by large solids. This bottom discharge pipe 17
may be provided in a plural number instead of a single number, or may be provided around the bottom of the overflow pipe 15.

分離後の被処理水を排水せしめる配水部として
の放流口18は水槽側で流入筒14の流入口より
も最もはなれたパスラインの長い位置で底部より
上方で、オーバーフロー管15の上端より下方に
開口している。
The outlet 18, which serves as a water distribution section for discharging the water to be treated after separation, is located above the bottom at the longest pass line farthest from the inlet of the inflow pipe 14 on the water tank side, and below the upper end of the overflow pipe 15. It's open.

前記放流口18をこの位置に設ける理由は次の
点にある。流入口から流入する下水に含まれてい
る固形物は、施回流と二次流れによつて沈殿性の
固形物は底部に沈殿し、浮上性の固形物は水面上
の中心部に浮上するので、上記放流口の位置では
側壁13に近い水には固形物が比較的少なくなつ
ている。この現象は、水流の観測によつて得た知
験に基づくものである。
The reason for providing the outlet 18 at this position is as follows. The solids contained in the sewage that flows in from the inlet are caused by circulation flow and secondary flow, with sedimentable solids settling to the bottom and floating solids floating to the center above the water surface. At the location of the outlet, the water near the side wall 13 contains relatively few solids. This phenomenon is based on knowledge gained from observing water flow.

この放流口18の付近の水流の状況を説明する
と、水流は側壁13に沿つて旋回しており、固形
物は旋回流によつて旋回方向の力を持つており、
放流口18の付近でもそのまま側壁に沿つて流れ
るが、水は水位によつて放流口18の方に流れる
が固形物を同伴しない。その理由は、固形物と水
とが旋回流により与えられる慣性力の影響の差に
よるもので固形物は水のように急激な方向転換が
できないことによるものと考えられる。
To explain the state of the water flow near the outlet 18, the water flow is swirling along the side wall 13, and the solid matter has a force in the swirling direction due to the swirling flow.
Even in the vicinity of the outlet 18, the water flows along the side wall as it is, but depending on the water level, the water flows toward the outlet 18, but solid matter is not entrained therein. The reason for this is thought to be due to the difference in the influence of inertial force exerted by the swirling flow between solids and water, and that solids cannot change direction as quickly as water.

放流口の下流側には放流堰19を設けて規定水
量以上の水量が流入して水槽の水位が放流堰19
の上端に達したときに初めて、この放流堰19か
ら越流水を放流路に流すようにしてある。この堰
は、降雨時の初期において有機物濃度の高い汚濁
物が流入するいわゆるフアーストフラツシユ現象
が起きるので、この初期に流入する汚濁物(固形
物)を越流させないでオーバーフロー管底部排出
管から下水処理場に流すためのものである。
A discharge weir 19 is provided on the downstream side of the discharge port, and when water exceeding the specified amount flows in, the water level of the tank is raised to the discharge weir 19.
The overflow water is allowed to flow from this discharge weir 19 into the discharge channel only when it reaches the upper end of the discharge weir. The so-called first flush phenomenon occurs in which pollutants with a high concentration of organic matter flow into this weir at the beginning of a rainfall. It is meant to be sent to a treatment plant.

図中、20は波動を防止するための安定板であ
る。オーバーフロー管15の上端からの安定板2
0の高さは、オーバーフロー量、旋回速度等によ
り適宜選ばれる。第4図に示す位置よりも低く、
オーバーフロー管15の上端からわずか上の位置
でもよい。作用につき説明すれば、流入下水(廃
水)は流入筒14の流入口により槽内下部に導入
し、側壁13に沿つて旋回し流入水量が増加する
につれて槽内の水位は上昇し水位がオーバーフロ
ー管15の上端に達するとオーバーフロー管15
の上端から下方に流れて槽外に流出する。
In the figure, 20 is a stabilizing plate for preventing wave motion. Stabilizer plate 2 from the upper end of the overflow pipe 15
The height of 0 is appropriately selected depending on the overflow amount, rotation speed, etc. Lower than the position shown in Figure 4,
The position may be slightly above the upper end of the overflow pipe 15. To explain the operation, inflowing sewage (wastewater) is introduced into the lower part of the tank through the inlet of the inflow tube 14, swirls along the side wall 13, and as the amount of inflow water increases, the water level in the tank rises and the water level reaches the overflow pipe. When reaching the upper end of 15, the overflow pipe 15
It flows downward from the top of the tank and out of the tank.

なお、放流堰19の上端まで水位が上つた場合
には、放流堰19から放流路に水が流れる。
Note that when the water level rises to the upper end of the discharge weir 19, water flows from the discharge weir 19 to the discharge channel.

この間に下水(廃水)中に含まれる固形物のう
ち沈砂分或いは沈殿性固形物は、重力と槽内の旋
回流とこれによつて生ずる二次流れの流体力によ
つて槽の底部に沈殿しながら槽の中央底部に集め
られ、底部排出管17から水と一緒に槽外に排出
される。
During this time, among the solids contained in the sewage (wastewater), the sediment content or settleable solids settle to the bottom of the tank due to gravity, the swirling flow in the tank, and the fluid force of the secondary flow generated by this. At the same time, the water is collected at the center bottom of the tank, and is discharged from the bottom discharge pipe 17 together with water to the outside of the tank.

水面に浮上した浮上性固形物は槽内に流入して
旋回流によつて旋回しながら浮上して槽中心部に
設けたオーバーフロー管15の上端部に集まる。
この際に槽内に発生する二次流れ21によつて浮
上性固形物は浮上が促進される。これはオーバー
フロー管15の周囲で底部から水面に向かつて上
昇する二次流れに起因すると考えられる。水面に
浮上した浮上性固形物は自由表面からオーバーフ
ロー管に流入する流れに同伴されて槽の外部に排
出され下水管を経て下水処理場に送られる。固形
物を除去された下水は水槽側壁13に設けた放流
口18から放流堰19を越えて放流路に流れる。
The floating solids floating on the water surface flow into the tank, float while swirling due to the swirling flow, and collect at the upper end of an overflow pipe 15 provided at the center of the tank.
At this time, the floating solids are promoted to float due to the secondary flow 21 generated in the tank. This is considered to be due to the secondary flow rising around the overflow pipe 15 from the bottom toward the water surface. The floating solids floating on the water surface are carried by the flow flowing from the free surface into the overflow pipe, are discharged outside the tank, and are sent to the sewage treatment plant via the sewer pipe. The sewage from which solids have been removed flows from a discharge port 18 provided in the side wall 13 of the water tank, over a discharge weir 19, and into a discharge channel.

〔発明の効果〕〔Effect of the invention〕

本発明は、側壁と底壁とで水平断面が円形状又
はスパイラル形状に構成した槽に、前記側壁に対
して接線方向に被処理水を流入せしめる流入口を
設けると共に、槽中央部に直立して上端が開放さ
れ、かつ下端が前記底壁を貫通している浮上物オ
ーバーフロー管と、前記側壁又は底壁の一部から
分離後の被処理水を排水せしめる排水部とを配備
したことにより、浮上物を水面中心に集めて比重
の小さな浮上性固形物の分離率が良いし、比重の
小さな浮上性固形物を降雨中常時槽外に有効に排
出できて下水処理場で処理することができると共
に、比重の大きな沈殿物は水槽底面に堆積するこ
となく底部から槽外に効率よく排出することがで
きる。即ち、二次流れが発達しているために底面
に沈降した固形物は二次流れによつて槽の中心方
向へ流動し集積されるために濃縮されて底部排出
管から槽外に排出され、さらに水槽の底部を中心
部が外周部より低くなるように傾斜させると二次
流れは一層強くなり分離効果を向上させると共
に、沈殿物を中央部に集積する度合も強くなつて
濃縮されて底部排出管から有効に排出されるし、
しかも機構が簡単なために固形物がつまりにく
く、保守も簡略化でき、さらに浮上性固形物が有
効に確実に分離除去ができる有用な効果を奏する
ことができる。
The present invention provides a tank having a side wall and a bottom wall with a circular or spiral horizontal cross section, and is provided with an inlet for allowing water to be treated to flow in in a tangential direction to the side wall, and an inlet which stands upright in the center of the tank. By providing a floating object overflow pipe whose upper end is open and whose lower end penetrates the bottom wall, and a drainage section that drains the separated water to be treated from a part of the side wall or the bottom wall, The floating solids are collected at the center of the water surface, resulting in a good separation rate for floating solids with low specific gravity, and the floating solids with low specific gravity can be effectively discharged outside the tank at all times during rain, allowing them to be treated at a sewage treatment plant. At the same time, precipitates having a large specific gravity can be efficiently discharged from the bottom of the tank to the outside of the tank without being deposited on the bottom surface of the tank. That is, because the secondary flow is developed, the solids that have settled on the bottom surface flow toward the center of the tank due to the secondary flow, are concentrated, and are discharged from the bottom discharge pipe to the outside of the tank. Furthermore, by sloping the bottom of the water tank so that the center is lower than the outer periphery, the secondary flow becomes stronger, improving the separation effect, and the degree to which sediment accumulates in the center increases, concentrating it and discharging it to the bottom. effectively discharged from the pipe,
In addition, since the mechanism is simple, it is difficult for solid matter to become clogged, maintenance is simplified, and furthermore, the floating solid matter can be effectively and reliably separated and removed, which is a useful effect.

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

第1図は従来のスワール分水槽の例の平面図、
第2図はその一部断面正面図、第3図は本発明の
実施例の平面図で第4図の―線断面図、第4
図は第3図の―線断面正面図である。 1…外殻、2…流入渠、3…流向制御板、4…
ダウンシヤフト、5…集水盆、6…越流堰、7…
スカムリング、8…スポイラー、9…スカムトラ
ツプ、10…汚水排出管、11…導溝、12…処
理水排水管、13…側壁、14…流入筒、15…
オーバーフロー管、16…底壁、17…底部排出
管、18…放流口、19…放流堰、20…安定
板、21…二次流れ。
Figure 1 is a plan view of an example of a conventional swirl water tank.
FIG. 2 is a partially sectional front view thereof, FIG. 3 is a plan view of an embodiment of the present invention, and FIG.
The figure is a sectional front view taken along the line -- in FIG. 3. 1...Outer shell, 2...Inflow conduit, 3...Flow direction control plate, 4...
Downshaft, 5...water collection basin, 6...overflow weir, 7...
Scum ring, 8... Spoiler, 9... Scum trap, 10... Sewage discharge pipe, 11... Guide groove, 12... Treated water drain pipe, 13... Side wall, 14... Inflow pipe, 15...
Overflow pipe, 16...bottom wall, 17...bottom discharge pipe, 18...discharge port, 19...discharge weir, 20...stabilizer, 21...secondary flow.

Claims (1)

【特許請求の範囲】 1 側壁と底壁とで水平断面が円形状に構成した
槽に、前記側壁に対して接線方向に被処理水を流
入せしめる流入口を設けると共に、槽中央部に直
立して上端が開放され、かつ下端が前記底壁を貫
通している浮上物オーバーフロー管と、前記側壁
又は底壁の一部から分離後の被処理水を排水せし
める排水部とを配備したことを特徴とする固液分
離装置。 2 前記排水部が、前記側壁の中間高さに設けら
れた放流口である特許請求の範囲第1項記載の装
置。 3 側壁と底壁とで水平断面が円形状に構成した
槽に前記側壁に対して接線方向に被処理水を流入
せしめる流入口を設けると共に、槽中央部に直立
して上端が開放され、かつ下端が前記底壁を貫通
している浮上物オーバーフロー管と、前記側壁又
は底壁の一部から分離後の被処理水を排水せしめ
る排水部と、前記オーバーフロー管の貫通部の付
近に設けた沈殿物排出口とを配備したことを特徴
とする固液分離装置。 4 前記排水部が前記側壁の中間高さに設けられ
た放流口である特許請求の範囲第3項記載の装
置。
[Scope of Claims] 1. A tank having a circular horizontal cross section with a side wall and a bottom wall is provided with an inlet that allows the water to be treated to flow in in a tangential direction to the side wall, and an inlet that is erect in the center of the tank. A floating object overflow pipe whose upper end is open and whose lower end penetrates the bottom wall, and a drainage section for draining the separated water to be treated from a part of the side wall or the bottom wall are provided. Solid-liquid separation equipment. 2. The device according to claim 1, wherein the drainage section is a discharge port provided at an intermediate height of the side wall. 3 A tank having a side wall and a bottom wall having a circular horizontal cross section is provided with an inlet for allowing the water to be treated to flow in in a tangential direction to the side wall, and stands upright in the center of the tank with an open top end, and A floating matter overflow pipe whose lower end penetrates the bottom wall, a drainage section for draining the separated treated water from a part of the side wall or the bottom wall, and a sedimentation area provided near the penetration section of the overflow pipe. A solid-liquid separator characterized in that it is equipped with a material discharge port. 4. The device according to claim 3, wherein the drainage portion is a discharge port provided at an intermediate height of the side wall.
JP19188782A 1982-11-02 1982-11-02 Solid-liquid separator Granted JPS5982988A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP19188782A JPS5982988A (en) 1982-11-02 1982-11-02 Solid-liquid separator
US06/538,992 US4517091A (en) 1982-11-02 1983-10-04 Solids-liquid separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19188782A JPS5982988A (en) 1982-11-02 1982-11-02 Solid-liquid separator

Publications (2)

Publication Number Publication Date
JPS5982988A JPS5982988A (en) 1984-05-14
JPH0143589B2 true JPH0143589B2 (en) 1989-09-21

Family

ID=16282104

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19188782A Granted JPS5982988A (en) 1982-11-02 1982-11-02 Solid-liquid separator

Country Status (1)

Country Link
JP (1) JPS5982988A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR3049197B1 (en) * 2016-03-24 2020-04-10 Kwi International Environmental Treatment Gmbh DISSOLVED AIR FLOAT

Also Published As

Publication number Publication date
JPS5982988A (en) 1984-05-14

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