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JPS59115710A - Solid-liquid separating device - Google Patents

Solid-liquid separating device

Info

Publication number
JPS59115710A
JPS59115710A JP22385882A JP22385882A JPS59115710A JP S59115710 A JPS59115710 A JP S59115710A JP 22385882 A JP22385882 A JP 22385882A JP 22385882 A JP22385882 A JP 22385882A JP S59115710 A JPS59115710 A JP S59115710A
Authority
JP
Japan
Prior art keywords
tank
water
sewage
solids
center
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.)
Granted
Application number
JP22385882A
Other languages
Japanese (ja)
Other versions
JPS6235803B2 (en
Inventor
Isao Kataoka
勲 片岡
Tetsuo Goto
哲郎 後藤
Koichi Yamanaka
山中 行一
Masanori Aoki
正則 青木
Toshiaki Nishiwaki
西脇 俊明
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 JP22385882A priority Critical patent/JPS59115710A/en
Priority to US06/538,992 priority patent/US4517091A/en
Publication of JPS59115710A publication Critical patent/JPS59115710A/en
Publication of JPS6235803B2 publication Critical patent/JPS6235803B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Centrifugal Separators (AREA)
  • Cyclones (AREA)
  • Removal Of Floating Material (AREA)

Abstract

PURPOSE:To send a concentrated solid matter independent of the quantity of water, to a sewage treatment plant by providing a tailrace of treated water to a shell part, a discharging part of suspended matter to an upper part, a discharging part of sediment to the bottom center, and an upright cylindrical body to the center, in a solid-liquid separation where a centrifugal force of sewage, etc. is utilized. CONSTITUTION:A sewage, flowed tangentially into a separation tank 2 from an inflow pipe 24, whirls 40 in the inside. At that time, the sewage flows downward along the side wall 22, flows upward at the central part, flows radially toward the outer circumference at the water surface, and flows toward the center at the bottom. The water after passing a screen 9 flows over an overflow weir 31 and is discharged from a pipe 22. The suspended matter at the upper part flows over an upper edge of an overflow trough 49 and is sent to a sewage treating plant. The sediment collected at the bottom is also sent to the sewage treating plant through a pipe 26. Further, a vertical convection current is made smooth by providing an upright cylindrical body 50 and stabilizer plates 38, 39 to the center. The solid-liquid separating capacity of a water to be treated is improved by using this device.

Description

【発明の詳細な説明】 本発明は、下水なとの如く、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なう固液分離装置に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a solid-liquid separator that performs solid-liquid separation of water to be treated, such as sewage and other types of wastewater containing solids.

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。
Overflow water discharged untreated from combined sewer systems during rainy days poses an important problem as a source of water pollution in public waters.

越流水質を改善するために、合流式F水越流調整装置は
2つの働きを強めるような下水道システムが必要となる
。この2つの役割とは、下水中の固形物を濃縮して下水
処理場へ送ることと雨天時の過剰な下水を放流l]に分
流することであり、これにより下水処理場へ送る流量を
処理能力以内に抑え、また河川へ放流する水の質を良好
にする、というmと質の制御を行なう。
In order to improve overflow water quality, a combined F water overflow adjustment device requires a sewerage system that strengthens two functions. These two roles are to condense solids in sewage and send it to the sewage treatment plant, and to divert excess sewage during rainy days to the effluent, thereby treating the flow rate sent to the sewage treatment plant. Water quality is controlled to keep water within capacity and to improve the quality of water discharged into rivers.

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ある。
A so-called swirl water diversion tank has been conventionally used as a solid-liquid separation device for use in this overflow regulating device.

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F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県、3は流入下水を槽の
周辺部の長い距離をとって旋回させるための流向制御板
、4は処理水を排11けるために槽の底部に垂IUに設
けられた管(ダウンシャフト)、5はダウンシャフト・
1の頂部に取f;jけられた集水盆、6は集水盆5の周
縁に取イ・1けられた越流せき、7は越流せき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。
An example of a swirl water tank is shown in Figures 1 and 2.
2 is the outer shell of the cylindrical swirl water diversion tank, 2 is the inlet that is located at the F section of the water diversion tank and introduces inflow sewage or wastewater containing pollutants into the tank in a tangential direction, and 3 is the inflow sewage tank. A flow direction control plate for rotating a long distance around the periphery of the tank, 4 a pipe (down shaft) installed in the vertical IU at the bottom of the tank to drain treated water, and 5 a down shaft.
A water collection basin is installed at the top of 1, 6 is an overflow weir installed at the periphery of the water collection basin 5, and 7 is an overflow weir installed around the outer periphery of the overflow weir 6. This is a scum ring placed at a distance to block scum floating on the water surface.

8はスポイラ−で、集水盆5にスカムリング7を連結し
集水盆」二及びスカムリングと越流せき開の水の回転エ
ネルギーを減少させてダウンシャフトの容量を増し、固
液分離効率を高めるものである。9は水面浮」ユ性物質
を捕集上これを集水貧5の下へ導くためのスカムトラッ
プ、1()は汚水排水管、]1は晴天時に固形物の堆積
するのを防止するために流入県2と汚水11:zkIi
!i’ I Oとを結びつけて、槽の床」二に設けられ
た導溝で、12は処理水排出管である。
8 is a spoiler, which connects the scum ring 7 to the water collection basin 5 to reduce the rotational energy of the water in the water collection basin 2, scum ring, and overflow dam, increasing the capacity of the down shaft, and increasing the solid-liquid separation efficiency. It enhances the 9 is a scum trap that collects solid substances floating on the water surface and guides them to the bottom of the water collection 5; 1 () is a sewage drain pipe;] 1 is to prevent solids from accumulating on sunny days. Inflow prefecture 2 and sewage 11:zkIi
! 12 is a treated water discharge pipe.

上記の如き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なわれる。
Treatment of inflowing sewage (or wastewater) by the swirl water diversion tank having the above structure is carried out as follows.

流入下水はスワール分水槽の下部に設けられた流入県2
から槽内に接線方向に導入され、流向制御板3によって
ダ・ンンシャフト4を中心に旋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
重力と慣性カによって沈降して槽の中央部に集められ、
汚水4I[小管1()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せき6の上縁を越えて集水盆
5に集り、スポイラ−8により回転エネルギーを減少さ
せられ、グ′ンンシャフト4を通じて、処理水として処
理水排出管12がら朝出される。
Inflow sewage is fed to Inflow Prefecture 2 installed at the bottom of the Swirl water tank.
The sewage is introduced into the tank in a tangential direction, and is raised through the tank while being rotated around the shaft 4 by the flow direction control plate 3. During this time, the sedimented sediment or suspended solids in the sewage are absorbed by gravity and inertia. It settles and collects in the center of the tank,
Sewage 4I [is discharged through small pipe 1 (). The sewage from which sedimentary suspended matter has been removed is filtered by the scum ring 7 to remove the floating substances, and the clear water is removed by the scum ring 7.
The water passes through the lower edge, crosses the upper edge of the overflow weir 6, and collects in the collection basin 5, whose rotational energy is reduced by the spoiler 8, and is discharged as treated water from the treated water discharge pipe 12 through the gun shaft 4 in the morning. Served.

前記スカl、リング7でさえぎられた水面汀」二性物質
は、スカムリング周囲を浮遊してスカムトラップ!〕で
捕集され、水流によって集水盆5の4r +=引きこま
れ、越流ぜき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がら排出される
The water surface blocked by the scum ring 7, the bisexual substance floats around the scum ring and becomes a scum trap! ], the water is drawn into the water collection basin 5 by the water flow, and is stored inside the portion of the water collection basin where the overflow weir 6 extends downward. 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 through 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「水が案内溝に沿って
直接汚水管へと導かれ下水処理場に運ばれる。雨入時の
流入量が多くなり水槽内の水位が高くなった時には、o
if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訊は少なくなり、オリイ
スから汚水管へ送られる。他方残りの清澄な下水は量が
多く越流せぎを越えていく。放流光の水質基準によって
この越流水はさらに処理されるがあるいは放流される、
二と1こなる。
In sewage treatment using such a swirl diversion tank, when the amount of water is low on sunny days, all the inflow water is guided directly to the sewage pipe along the guide groove and transported to the sewage treatment plant.When it rains, the amount of inflow water is When the water level in the aquarium increases due to the increase in o
Separate the solids as described if. The amount of highly concentrated sewage containing a large amount of solid matter becomes less concentrated as a result of concentration, and is sent from the Orys to the wastewater pipe. On the other hand, the remaining clear sewage water is large in volume and flows over the overflow stream. This overflow water can be further treated or discharged according to the water quality standards of the discharge light.
Two and one.

と5:ろが、このスワール分水槽は次の如き欠点を有す
る。
5: However, this swirl water tank has the following drawbacks.

(1)比重が1より小ル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
ては分離機能は持っているが水槽の水位か低下しないと
排出敗北が作用しなり・ために貯留能力に限界がある。
(1) Separation rate of floating objects with specific gravity less than 1 is poor. Although it has a separation function for floating solids (commonly known as S and S) with a specific gravity of less than 1, there is a limit to the storage capacity because if the water level in the tank does not decrease, the discharge will fail.

そのためにこれを超えた場合、放流(越流)水中に浮遊
物が混しって流出し結果として分離性能が低下している
Therefore, if this value is exceeded, suspended matter is mixed with the discharged (overflow) water and flows out, resulting in a decrease in separation performance.

水槽の水位が上列して越流する状況にある場合、スカム
リング7の下端から越流せき6に流入する流速が速くな
り、この速い流れに浮」二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1丁する。流
速の速くなる原因は、流入量が汚水JI+出管小管から
流出する訊より大11】に増加したときに水位が」ニカ
して越流する水量であるから水量としては火各いものと
なるためである。
When the water level in the water tank is rising and overflowing, the velocity of the flow flowing from the lower end of the scum ring 7 into the overflow weir 6 becomes faster, and this fast flow carries the dimorphic solids that float in the treated water. Since it flows out into the discharge pipe 12, the separation efficiency is low. The reason why the flow rate becomes faster is that when the inflow volume increases to 11 times larger than the amount of sewage flowing out from the sewage JI + outflow pipe, the water level rises and the amount of water overflows, so the amount of water becomes fiery. It's for a reason.

(2)浮上物の分離排出を常時性なうことがで外ない。(2) It is inevitable that floating objects must be separated and discharged constantly.

例えば降雨時に常時性なうことかで外ない。For example, it is natural that it occurs constantly during rainy weather.

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っていない1.なんとならば、
この固形物は水に浮んC゛おり、漕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−L昇して
から流入する下水に含まれている浮に性固形物はスカム
トラップ9で捕集されるよりもスカムリングの下端から
越流せきを越えて流れる流れ(流速が速いので)に同伴
される量のノjが多くなる。
Swirl type water tank simply stores the separated floating solids in the lower part of the water collection basin, and does not have the function of discharging them to the outside of the water tank until the water level drops.1. If anything,
This is because the solids float in the water and are blocked by a layer of water between the sewage discharge pipe provided at the bottom of the tank and the lower layer of the accumulated solids. Therefore, the floating solids contained in the inflowing sewage after the water level rises by -L are collected by the flow that flows from the lower end of the scum ring over the overflow weir (with a high flow rate) rather than being collected by the scum trap 9. Therefore, the amount of energy that is accompanied by ) increases.

(3)沈殿物の排出が困難である。(3) It is difficult to discharge the precipitate.

浮」−性固形物を捕集するスカl、トラップやスカムリ
ングを設けているために槽内の二次流れの発達を1;1
1書する。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ホリ汚水排出管の開[1部まで移動
することは少ない。従って晴天時に坩積物を人手でシI
°除するなどの保守か必要となる (4)固形物がつまり易い。
A scum ring, trap, and scum ring are installed to collect floating solids, which reduces the development of secondary flow within the tank.
Write one book. Therefore, solids with a large specific gravity settle at the bottom and rarely move to the open part of the sewage discharge pipe. Therefore, when the weather is clear, the crucibles are manually removed.
Maintenance such as cleaning is required (4) Solids can easily clog.

スワール型ではスカムリング、スカムトラップなどを設
けているために大きな固形物がこれらにからまってつま
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 with these and become clogged.

本発明は、従来のものの」−記の欠点を除き、浮−L性
固形物を水面に集めると共に沈殿性固形物を底面中央に
集めて有効に排出することかで外、かつその排出作業を
降雨中でも常時行なうことがで訃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 the drawbacks of the conventional ones, by collecting floating solids on the surface of the water and collecting settling solids in the center of the bottom surface for effective discharge. The object of the present invention is to provide a solid-liquid separator that can be operated continuously even in rainy weather.

本発明は、はぼ円形の側壁と底面とを有する槽に、前記
側壁に月して接線力向に被処理水を流入せしめる流入[
」と、前記側壁の一部又は前記底面の一部との少なくと
も一方に分離処理後の処理済み水を槽外に導く放流に1
と、前記底面のほぼ中央部に分離した沈殿性固形物を多
く含む濃縮液を槽外に導く沈殿性固形物排出部と、前記
側壁の−1一部をオーバーフローせしめて浮遊性固形物
を多く含む濃縮液を槽外に導く浮遊性固形物排出部とを
備えていることを特徴とする固液分離装置である。
The present invention provides an inflow system in which water to be treated flows into a tank having approximately circular side walls and a bottom surface in a tangential direction to the side walls.
”, and at least one of the side wall and the bottom surface is connected to a discharge area for guiding the treated water after separation treatment to the outside of the tank.
and a precipitable solids discharge part that guides the concentrated liquid containing a large amount of separated precipitable solids to the outside of the tank, approximately in the center of the bottom surface, and a -1 part of the side wall that overflows to collect a large amount of suspended solids. This solid-liquid separator is characterized by comprising a floating solids discharge section that guides the concentrated liquid contained therein to the outside of the tank.

本発明の実施例を図面を用いて説明する。Embodiments of the present invention will be described using the drawings.

ff13図ないし第5図において、分^1[槽21は、
はぼ円形(円形、楕円形、長円形などの類似円形成いは
スパイラル状)の側壁22及び底面2:(を有しζいる
。この分離4V’i21には被処理液を側壁22に月し
て接線方向に導入して分離槽21内における液に旋回運
動をりえるよう流入管路24の流入112 !’iを側
壁22に設ける。流入1125の位置は、一部か底面2
3にかかつてもよく、又、底部2;(のみにあってもよ
い。底面23は外周から中心に向って傾斜している。底
面23は水平面に形成してよいか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
ff In Figures 13 to 5, minute^1 [tank 21 is
It has a side wall 22 and a bottom surface 2 of a substantially circular shape (a similar circular shape such as a circle, an ellipse, an ellipse, or a spiral shape). The inflow 112!'i of the inflow pipe 24 is provided on the side wall 22 so that the liquid in the separation tank 21 can be introduced in a tangential direction and given a swirling motion to the liquid in the separation tank 21.
The bottom surface 23 may be sloped from the outer periphery toward the center. A slope is more effective for accumulating at the center of the bottom.

分^II槽21の底面23の中央には底部排出管26を
設け、被処理液に含まれている沈殿性の固形物を後述の
如く、旋回流及び二次流により底部に集積、分離して濃
縮された被処理液と共に槽外に11出するものである。
A bottom discharge pipe 26 is provided at the center of the bottom surface 23 of the II tank 21, and the precipitable solids contained in the liquid to be treated are collected and separated at the bottom by swirling flow and secondary flow, as described later. The tank is then discharged to the outside of the tank together with the concentrated liquid to be treated.

又分離槽21に流入する液量が減少した場合には、槽内
に貯留している固液はこれより槽外に排出される。
Furthermore, when the amount of liquid flowing into the separation tank 21 decreases, the solid liquid stored in the tank is discharged to the outside of the tank.

分離槽21の側壁22の一■一部を−・部切欠いてオー
バーフロー樋45)を設けて浮遊性固形物排出部が形成
されている。オーバー70−樋49は側壁22の−L部
の全周に設けて、全周からオーバー70−させるように
してもよい。これに、1−り、分離槽21の−に部に形
成される自由表面28近辺に集積される浮遊性の固形物
やスカムを、自由表面28h・r〕オーバー70−樋4
5月こ流入する被処理液と共に濃縮液として槽外に排出
する。
An overflow gutter 45) is provided by cutting out a part of the side wall 22 of the separation tank 21 to form a floating solids discharge section. The over 70 gutter 49 may be provided around the entire circumference of the -L portion of the side wall 22 so that it extends over the entire periphery. In addition, the floating solids and scum accumulated in the vicinity of the free surface 28 formed at the - side of the separation tank 21 are removed from the free surface 28h/r] over 70-gutter 4.
It is discharged to the outside of the tank as a concentrated liquid together with the liquid to be treated that flows in in May.

底部排水管26及びオーバーフロー樋49がら−・定量
の沈殿性及び浮遊性の固形物か連続的に槽外に除去され
るために分離槽21内の固形物濃度は」二限値を超える
ことはない。そのために分離槽21の固形物除去率は低
下せず又処理能力も低下することはない。底部排出管2
6とオーバーフロー樋49により、固形物を多く含む濃
縮液を槽外に導く濃縮液排出部を形成する。沈殿物又は
浮遊物が予め除かれていれば、何れが一方のみでよい。
Since a fixed amount of settled and floating solids are continuously removed from the bottom drain pipe 26 and overflow gutter 49 to the outside of the tank, the solids concentration in the separation tank 21 cannot exceed two limits. do not have. Therefore, the solid matter removal rate of the separation tank 21 does not decrease, nor does the processing capacity decrease. Bottom discharge pipe 2
6 and the overflow gutter 49 form a concentrated liquid discharge section that guides the concentrated liquid containing a large amount of solids to the outside of the tank. As long as the precipitates or suspended matter are removed in advance, only one of them may be used.

分離槽21の側壁22にはスクリーン2(」を有する放
流口が設けられている。このスクリーン29は槽外に放
流される液体に含まれる固形物をスクリーン面にf・1
着させて液体だけを通過させるためのものである。この
放流[−Jは槽側壁の周方向にも−にF力方向も適当な
長さを持たせる。火流鼠を処理するためには」二部り向
にそれぞれ火熱な(j°法をとるようにする。
The side wall 22 of the separation tank 21 is provided with a discharge port having a screen 2 ( ).
This is to allow only liquid to pass through. This discharge [-J has an appropriate length both in the circumferential direction of the tank side wall and in the force direction F. To deal with a fire rat, use the fire heat (J° method) in two directions.

スクリーン29を有する放流に1の位置は流入1−12
5から側壁22の内周に沿ってなるべく遠いガがよい。
1 position in the outlet with screen 29 inlet 1-12
5 along the inner periphery of the side wall 22 as far as possible.

書に記載された如外構造のものを用いる。Use the structure described in the book.

スクリーン29の下流側には越流せき31が設けられて
いる。分離槽21に流入する液体の流入量が一定値を超
えて分離槽21の水面がオーバー70−樋、49の越流
上縁に達してか呟越流せき31を越えて流出するように
設定することが好ましい。
An overflow weir 31 is provided downstream of the screen 29. The setting is such that when the amount of liquid flowing into the separation tank 21 exceeds a certain value and the water surface of the separation tank 21 reaches the upper edge of the overflow of the overflow gutter 49, the liquid flows out over the overflow weir 31. It is preferable to do so.

越流ぜき31のF流側には、越流管32を設けて河川等
に連結する。雨量が多くなって]ζ水処理場で処理可能
な量を超過した水量分を、汚濁物を除去して河川等に放
流することかでトる。
An overflow pipe 32 is provided on the F flow side of the overflow weir 31 and connected to a river or the like. This can be achieved by removing pollutants from water that exceeds the amount that can be treated at water treatment plants due to increased rainfall and releasing it into rivers, etc.

50は直立した柱状体により形成された渦防止部祠であ
り、自由表面28の中心に、旋回流による渦か゛発生す
るのを防止する作用を有する。また二次流れの上碧流が
安定して形成されるようになる。
Reference numeral 50 denotes a vortex prevention part shrine formed by an upright columnar body, and has the function of preventing a vortex from being generated at the center of the free surface 28 due to swirling flow. In addition, the secondary flow, Kamiheki-ryu, is stably formed.

38及び3つは安定板である。38 and 3 are stabilizers.

以」二の如き実施例の作用について説明する。The operation of the second embodiment will now be explained.

流入管路2・1を経て流入(]25より分離槽21内に
流入した下水は、槽内を矢印/1.1.1の方向に旋回
する旋回流となって循環し、その開に浮遊性固形物は水
面【こ)7上し、沈殿性固形物は底面23に沈殿する。
The sewage that has flowed into the separation tank 21 through the inflow pipe 2.1 (25) circulates in the tank as a swirling flow in the direction of the arrow /1.1.1, and floats in the opening. The solids rise above the water surface 7, and the precipitable solids settle on the bottom 23.

一方槽内の旋回流により、矢印41に示す如き、側壁2
2に沿って下降し、底面23に沿って中央に向かい、渦
防止部材50の外側に沿って−1−■化、自由表面28
に沿って周囲に向かって循環して流れる二次流れを生ず
る。底面23に沈殿した固形物は、底面2:(の傾斜に
よって重力により次第に集まる1【丁(向があるか、こ
の−4次流れによって一層短時間で中央に寄せ集められ
、底部411出管26より効果的に抽出される。
On the other hand, due to the swirling flow inside the tank, the side wall 2 as shown by the arrow 41
2, toward the center along the bottom surface 23, -1-■ along the outside of the vortex prevention member 50, and the free surface 28
This creates a secondary flow that circulates along the periphery. The solid matter that has settled on the bottom surface 23 gradually gathers due to gravity due to the slope of the bottom surface 2. extracted more effectively.

また、浮遊性の固形物は比較的軽いものはすく浮にして
オーバーフロー樋4つの越流L:縁からオーバーフロー
するが、比重が1に近いものは旋回流に巻外込まオして
なかなか浮上分離されない。しh化本実施例においては
−に記の如く二次流れが生ずるので、浮遊性固形物が自
由表面22;に導かれ、か−)k回;ズCにより、オー
バーフロー樋・↓!Jの越流上Hに達し易く、オーバー
70−による除去が容易に、〒、く行なわれる。側壁2
2の全周にてオーバーフローを行なう場合は、旋回流の
遠心力の作用にJ:り朝出か容易確実となる。
In addition, relatively light floating solids float to the top of the overflow gutter and overflow from the edge of the four overflow channels, but solids with a specific gravity close to 1 are swept up into the swirling flow and are easily separated by flotation. Not done. In this embodiment, a secondary flow occurs as shown in -, so the floating solids are guided to the free surface 22, and the overflow gutter ↓! The overflow of J can easily reach H, and removal by over 70- is easily performed. side wall 2
If overflow is performed around the entire circumference of 2, the centrifugal force of the swirling flow will cause the flow to flow easily and reliably.

本実施例においては、分^1[槽21の中には渦防市部
材:(()のみか設けられ、円滑な;ガこれを妨げるも
のはなく、しがち渦防止部4’4’ 30が、底部22
に沿って中央に向がって集って来る二次流れが互に衝突
して乱れるのを防ぎ、二次流れを整然と上ガ、流に方向
転換せしめることができるので、二次流れが強力に、確
実に形成される。
In this embodiment, only the vortex prevention member (() is provided in the tank 21, and there is nothing to disturb the smooth movement of the vortex prevention member 4'4'30). However, the bottom 22
It prevents the secondary flows that gather toward the center along the It is reliably formed.

しかして、底部偵°小管26及びオーバー70−樋4つ
から固形物を多く含んだ濃縮液を排出することにより固
形物を分離した処理済み水は、放流[1のスクリーン2
9のスリットを通過して槽外に流出し、河川に放流され
る。
The treated water from which solids have been separated by discharging the concentrated liquid containing a large amount of solids from the bottom conduit 26 and the four overspouts 70 is discharged to the screen 2 of [1].
It passes through slit 9 and flows out of the tank, and is discharged into the river.

この場合、分離槽21の設計値以−にの液量が流入した
場合あるいは、大量の固形物か混入している場合でも、
放流口に設けたスクリーン2′:3によって固形物の流
れを防ぎ、か−〕、−れら固形物を分gtc槽21に貯
留して分離槽21の底部あるいは]二部から液体と共に
濃縮液として槽タトに排出する。
In this case, even if the amount of liquid flowing into the separation tank 21 is higher than the design value, or if a large amount of solid matter is mixed in,
The flow of solids is prevented by a screen 2': 3 provided at the outlet, and the solids are stored in the separated GTC tank 21 and are collected together with the liquid from the bottom of the separation tank 21 or the two parts. It is discharged into a tank.

従って従来のロータリー型、かきあげ型自動除しん(幾
のように固形物を液体から完全に分離することがないの
で、ポンプ又はヘッドによる流木輸送を行なうことがで
き、従来の方法の如き除去した固形物を容器に入れて自
動車等で運搬するなどの手数はなく運転経費が低減でき
る。
Therefore, since the solids are not completely separated from the liquid as in the conventional rotary type or scraping type automatic descaling method, it is possible to transport the driftwood using a pump or head, and the solids removed as in the conventional methods are not completely separated from the liquid. There is no need to put things in containers and transport them by car, etc., and operating costs can be reduced.

分離槽21の設置位置によっては、放流1−1あるいは
底部排出管26、オ〜バー70−樋49から流出する液
体か自然放流できない場合はポンプによって押し出す。
Depending on the installation position of the separation tank 21, the liquid flowing out from the discharge 1-1, the bottom discharge pipe 26, and the over 70-gutter 49 may be pushed out by a pump if it cannot be discharged naturally.

その場合には、槽の各流出部とポンプの間に調節用に適
当な貯槽を設けるのが好ましい。
In that case, it is preferable to provide a suitable reservoir for regulation between each outlet of the tank and the pump.

第6図は別の実施例の流入nを示し流入口25は下辺か
底部23にて形成され内力に向は傾斜しているので、沈
降性固形物は傾斜の下方のノ入部に集まり、沈降性固形
物は流入1’:I 25を出てがら槽の中央に集まり易
<、#l=出が容易となる。
FIG. 6 shows the inlet n of another embodiment, and the inlet 25 is formed at the lower side or the bottom 23 and is inclined in the direction of the internal force. The solids tend to collect in the center of the tank while leaving the inflow 1': I25, #l=easy to exit.

第′7図は別の実施例の流入口25を示し、−1−辺の
天井板51が中心に向かって上がるように傾斜している
。浮遊性固形物は傾斜に沿って13の部分に集まり易く
、流入1」25を出てからすく)甲1ニし易く分離され
易い。下辺は水平で上辺のみ傾けてもよい。垂直壁52
及び天井板51はjltl+壁22よりもさらに槽内に
延長されていてもよい。
FIG. '7 shows an inlet 25 of another embodiment, in which the ceiling plate 51 on the -1- side is inclined upward toward the center. Floating solids tend to collect in the section 13 along the slope, and after leaving the inlet 25, they are easily separated. The bottom edge may be horizontal and only the top edge may be tilted. vertical wall 52
The ceiling plate 51 may extend further into the tank than the wall 22.

本実施例は以上の如く構成され作用するので、次の如き
効果を有する。
Since this embodiment is constructed and operates as described above, it has the following effects.

(1)比重の小さな浮」二性固形物の分It!Ill率
が良い。
(1) Float with a small specific gravity, fraction of dimorphic solids It! Good Ill rate.

(2)比重の小さな浮上性固形物を降雨中常時槽外に抽
出し、下1(処理場へ送ることができる(3)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常時
槽外に排出することかできる。
(2) Floatable solids with low specific gravity can be constantly extracted outside the tank during rain and sent to the treatment plant (3) Sediments with high specific gravity can be constantly extracted from the bottom of the tank without being deposited on the bottom of the tank. It can be discharged outside.

本実施例では、二次流れか発達している。そのために定
面に沈降した固形物は二次流れによって槽の中心方向へ
流動し集積されるために濃縮されて底部上1出管から槽
外に排出される。水槽の底部を第4図のように中心部か
外周より低くなるように傾斜させると二次流れは強くな
り分離効果を向」−させると共に、沈殿物を中央部に集
積する度合も強くなって濃縮されて底部排出管から排出
される。
In this example, a secondary flow is developed. Therefore, the solids that have settled on a constant surface flow toward the center of the tank by the secondary flow, are accumulated, are concentrated, and are discharged out of the tank from the top outlet pipe at the bottom. If the bottom of the tank is sloped so that it is lower than the center or the outer periphery as shown in Figure 4, the secondary flow will become stronger, improving the separation effect and increasing the degree to which sediment accumulates in the center. It is concentrated and discharged through the bottom discharge pipe.

(4)機構が簡単なために固形物か−)まりにくい。(4) Because the mechanism is simple, it is difficult for solid objects to get stuck.

本実施例は構成が極めて簡単なので、固形物がつまるお
それもなく、従って保守か簡略化できる。
Since the structure of this embodiment is extremely simple, there is no fear of solid matter clogging, and therefore maintenance can be simplified.

本発明により、沈殿性固形物のみならず浮−11性固形
物も併せ有効に確実に分離除去ができしかも降雨中でも
常時除去作業を行なうことができる固液分離装置を提供
することができ、実用上極めて大なる効果を奏すること
ができる。
According to the present invention, it is possible to provide a solid-liquid separator that can effectively and reliably separate and remove not only precipitable solids but also floating solids, and can perform removal work at all times even in the rain. Above all, it is possible to achieve a very large effect.

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

第1図は従来のスワール分水槽の例の平面図、第2し1
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、第4図はそのE −E線断面とF−F線断面とを
兼ねた断面図、第5図は第3図の(i−G線断面図、第
6図及び第゛7図はそれぞれ別の実施例で第5図のH−
H線断面相当図である。 1・・外殻、2・・流入県、3・・流向制御板、4・・
ダ1ンンシャフト、5・・集水盆、6・・越流せき、7
・・スカムリング、8・・スポイラ−153・・スカム
トラップ、10・・汚水排出管、11・・導溝、12・
・処理水排水管、21・・分離槽、22・・側壁、23
・・底面、24・・流入管路、25・・流入口、26・
・底部排出管、28・・自由表面、29・・スクリーン
、30・・除去(幾構、31J・越流せぎ、32・・越
流管、34・・スリット、38.3つ・・安定板、40
141・・矢1事1.=I り・・オーバー70−4;
献 50・・渦防11“部祠、51・・天井板、52・
・垂直壁。 特ii’1111 ’+ I煩人  株式会(1荏原製
1′に所代3111人弁+II+1・ T−Ill  
   稔第3図 第4図 −」 □ 一材一 22 38 .25 2 .38 51 5
Figure 1 is a plan view of an example of a conventional swirl water tank;
3 is a plan view of an embodiment of the present invention, FIG. 4 is a sectional view taken along lines E-E and F-F, and FIG. 3 (cross-sectional view taken along the line i-G, FIG. 6, and FIG.
It is a corresponding view of the H-line cross section. 1. Outer shell, 2. Inflow prefecture, 3. Flow direction control plate, 4.
Dam shaft, 5... Water collection basin, 6... Overflow weir, 7
・・Scum ring, 8・・Spoiler-153・・Scum trap, 10・・Sewage discharge pipe, 11・・Guiding groove, 12・・
- Treated water drain pipe, 21... Separation tank, 22... Side wall, 23
・・Bottom surface, 24・・Inflow pipe line, 25・・Inflow port, 26・
・Bottom discharge pipe, 28.・Free surface, 29.・Screen, 30.・Removal (multiple structures, 31J・Overflow girder, 32.・Overflow pipe, 34.・Slit, 38. 3・・Stabilizing plate) , 40
141...arrow 1 thing 1. =I ri...over 70-4;
Dedication 50... Uzuban 11" part shrine, 51... Ceiling board, 52...
・Vertical wall. Special ii'1111' + I-Kinjin Co., Ltd. (1 Ebara 1' with 3111 people's dialect + II + 1, T-Ill)
Minoru Figure 3 Figure 4-'' □ One piece of material 22 38. 25 2. 38 51 5

Claims (1)

【特許請求の範囲】 1、 はぼ円形の側壁と底面とを有する槽に、前記側壁
にス・1して接線方向に被処理水を流入せしめる流入1
−1と、111j記側壁の一部又は前記底面の 部との
少なくとち−・方に分離処理後の処理済み水を槽外に導
く放流口と、iYj記底前底面ぼ中央部に分離した沈殿
性固形物を多く含む濃縮液を槽外に導X沈殿性固形物請
出部と、1iij記側壁のに部をオーバー70−せしめ
て浮遊性固形物を多く含む濃縮液を槽外に導く浮遊性固
形物排出部とを備えていることを特徴とする固液分離装
置。 2、 はぼ円形の側壁と底面とを有する槽に、前記側壁
に対して接線力向に被処理水を流入ぜしぬる流入1−1
と、前記側壁の一部又は前記底面の一部との少なくとも
一方に分離処理後の処理済み水を槽外に導く放流口と、
前記底面のほぼ中央部に分離した沈殿+!1:固形物を
多く含む濃縮液を槽外に導く沈殿性固形物排出部と、前
記側壁の」二部をオーバーフローせしめて浮遊性固形物
を多く含む濃縮液を槽外に導く浮遊性固形物排出部とを
備え、かつ前記槽の中央に直立した柱状体を備えている
ことを特徴とする固液分離装置。
[Claims] 1. An inlet 1 for causing water to be treated to flow into a tank having a substantially circular side wall and a bottom surface in a tangential direction with respect to the side wall.
-1, a discharge port for guiding the treated water after the separation treatment to the outside of the tank at least in one of a part of the side wall or the bottom part in 111j, and a separation in the central part of the front bottom face in iYj. The precipitable solids discharge part and the part of the side wall described in 1iij are drawn over 70° to direct the concentrated liquid containing a large amount of suspended solids to the outside of the tank. A solid-liquid separator comprising: a floating solids discharge section for guiding the solid matter; 2. Inflow of water to be treated into a tank having approximately circular side walls and a bottom surface in a tangential direction to the side walls 1-1
and an outlet for guiding the treated water after the separation treatment to the outside of the tank, at least on one of the part of the side wall or the part of the bottom surface,
Precipitate separated approximately in the center of the bottom +! 1: A precipitable solids discharge part that leads a concentrated liquid containing a large amount of solids to the outside of the tank, and a floating solids discharge part that causes a two part of the side wall to overflow and leads a concentrated liquid that contains a large amount of floating solids to the outside of the tank. What is claimed is: 1. A solid-liquid separator comprising: a discharge section; and a columnar body standing upright in the center of the tank.
JP22385882A 1982-11-02 1982-12-22 Solid-liquid separating device Granted JPS59115710A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP22385882A JPS59115710A (en) 1982-12-22 1982-12-22 Solid-liquid separating device
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
JP22385882A JPS59115710A (en) 1982-12-22 1982-12-22 Solid-liquid separating device

Publications (2)

Publication Number Publication Date
JPS59115710A true JPS59115710A (en) 1984-07-04
JPS6235803B2 JPS6235803B2 (en) 1987-08-04

Family

ID=16804808

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22385882A Granted JPS59115710A (en) 1982-11-02 1982-12-22 Solid-liquid separating device

Country Status (1)

Country Link
JP (1) JPS59115710A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018130823A (en) * 2017-02-13 2018-08-23 アピュアン株式会社 Impact device, impact force adjustment method for impact device, and impact sound frequency adjustment method for impact device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018130823A (en) * 2017-02-13 2018-08-23 アピュアン株式会社 Impact device, impact force adjustment method for impact device, and impact sound frequency adjustment method for impact device

Also Published As

Publication number Publication date
JPS6235803B2 (en) 1987-08-04

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