JP2006037510A - Rainwater reservoir facility in sewerage and its method - Google Patents

Rainwater reservoir facility in sewerage and its method Download PDF

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JP2006037510A
JP2006037510A JP2004219000A JP2004219000A JP2006037510A JP 2006037510 A JP2006037510 A JP 2006037510A JP 2004219000 A JP2004219000 A JP 2004219000A JP 2004219000 A JP2004219000 A JP 2004219000A JP 2006037510 A JP2006037510 A JP 2006037510A
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screen
rainwater
water tank
water
solid
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Takashi Ochi
崇 越智
Akira Nakabayashi
昭 中林
Katsumi Moritsubo
克己 森坪
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Tsukishima Kikai Co Ltd
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Tsukishima Kikai Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To reduce a cleaning frequency in a rainwater reservoir pond. <P>SOLUTION: This invention relates to a rainwater reservoir facility in a confluent type sewerage for introducing sewage and rainwater to a sewage treatment plant 2 by a common trunk flow passage. An overflow dam 3 is arranged in the trunk flow passage 1, and overflow water from this overflow dam 3 is taken in, and the taken-in overflow water is sent in the tangent direction of a screen 51 into the cylindrical screen 51 arranged in the vertical direction inside a cylindrical water tank 50, and a vortex flow is generated in the screen 51. While the liquid content is sent outside the water tank 50 via the screen 51 and is supplied to the rainwater reservoir pond 6, the solid content is gathered to a central lower part of the water tank 50, and this gathered solid content is extracted outside the water tank 50. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、下水を幹線流路を介して下水処理場に導き処理する下水道システムにおける、雨水滞水技術に関する。   The present invention relates to a rainwater stagnant technique in a sewer system that guides and treats sewage to a sewage treatment plant via a main channel.

下水道には、雨水と汚水とを別の管渠で処理設備へ排水するように構成されている分流式下水道と、同一の管渠で処理設備へ送水する合流式下水道とがある。合流式下水道は管渠が一系統で済み、施工が容易で安価であることから、下水道設備の急速な普及が進んだ明治後期から昭和前期に大都市を中心に自治体に多く採用されており、現在広く普及している。   There are two types of sewerage: a sewer sewer that is configured to drain rainwater and sewage to the treatment facility using separate pipes, and a combined sewer that supplies water to the treatment equipment using the same pipe. The combined sewer system has been adopted by local governments mainly in large cities from the late Meiji period to the early Showa era, as the sewerage system has only one system, is easy to construct, and is inexpensive. Currently widely used.

合流式下水道では、雨天時に処理許容量を超える多量の雨水が下水処理場に流れ込むことがあり、従来は、このような許容量を超えた分を、通常の処理経路とは別経路に越流させ、この越流水を未処理もしくは目の粗いスクリーン等の簡易処理で川や海等の公共用水域に放流している。しかし、このような未処理若しくは簡易処理の越流水を放流するのは環境負荷や衛生の観点から好ましくないことはいうまでもない。   In combined sewers, a large amount of rainwater that exceeds the processing allowance may flow into the sewage treatment plant during rainy weather. Conventionally, the amount exceeding the allowable capacity overflows to a separate route from the normal processing route. The overflow water is discharged into public water areas such as rivers and seas by simple treatment such as untreated or coarse screens. However, it goes without saying that discharging such untreated or simplified treated overflow water is not preferable from the viewpoint of environmental load and hygiene.

このような観点から、雨天時の越流水対策として雨水滞水池を設置することが行われている(例えば特許文献1参照)。雨水滞水池は、雨天時越流水の一部を貯留するものであり、貯留水を降雨終了後に下水処理設備に送水して処理することにより、合流式下水道から排出される雨天時放流負荷量の削減、越流回数の削減などを図ることができる。   From such a point of view, installation of a rainwater catchment pond has been carried out as a measure against overflowing water in rainy weather (see, for example, Patent Document 1). A rainwater reservoir is a part of the rainwater overflow, which is used to store the amount of rainwater discharge load that is discharged from the combined sewer system by sending the stored water to the sewage treatment facility after the rain has ended. Reduction and the number of overflows can be reduced.

しかし、上記従来の雨水滞水池では、その貯留期間に、下水中に含まれる砂等の沈降し易い沈降性物質が池底部に堆積したり、夾雑物が壁面に付着したりし、これらが悪臭やハエ発生の原因となっていた。   However, in the conventional rainwater pond, the sedimentary substances such as sand contained in the sewage easily settle on the bottom of the pond or the foreign matter adheres to the wall surface during the storage period. And the cause of flies.

また、この問題点に対して、別途貯留しておいた洗浄水を降雨終了後に雨水滞水池内に勢い良く放出し洗浄する所謂フラッシュ洗浄(例えば特許文献2、3参照)や、雨水滞水池の前段にスクリーンや沈砂池(砂溜まり)を設け、雨水滞水池内に砂等が流入するのを防ぐことが提案されているが、いずれも不十分であった。   In addition, in order to solve this problem, so-called flush cleaning (see, for example, Patent Documents 2 and 3) in which separately stored wash water is discharged and washed into the rainwater reservoir after the rain has ended, It has been proposed that a screen and a sand basin (sand pool) be installed in the previous stage to prevent sand and the like from flowing into the rainwater pond.

そのため、従来は定期的に人手で清掃する必要があり、また雨水滞水池の多くが地下に設置されており且つ容積が大きいため、清掃に多大な手間と費用がかかるという問題点があった。   For this reason, conventionally, it has been necessary to periodically perform manual cleaning, and many rainwater reservoirs are installed underground and have a large volume, so that there is a problem that a lot of labor and cost are required for cleaning.

一方、分流式下水道においても、雨天時等において幹線流路の雨水を流量が増加した時には、別経路に越流させて放流または雨水滞水池に供給することが行われており、汚水が混じらないためハエが発生し難いことを除けば、砂や夾雑物が雨水滞水池に堆積・付着する等、基本的問題点は合流式と同様である。
特開平7−259745号公報 特開2004−116181号公報 特開平5−346016号公報
On the other hand, in the case of sewerage sewers, when the flow of rainwater in the main line increases in rainy weather, etc., it is carried over to another route to be discharged or supplied to the storm water reservoir, so that sewage is not mixed Therefore, except for the fact that flies are less likely to occur, the basic problems are the same as for the confluence type, such as sand and foreign matter accumulating and adhering to the rainwater reservoir.
Japanese Patent Laid-Open No. 7-259745 JP 2004-116181 A JP-A-5-346016

そこで、本発明の主たる課題は、雨水滞水池における清掃頻度の低減、維持管理の容易化を図ることにある。   Therefore, the main problem of the present invention is to reduce the frequency of cleaning and to facilitate maintenance in a rainwater reservoir.

上記課題を解決した本発明およびその作用効果は次記のとおりである。
<請求項1記載の発明>
下水を幹線流路を介して下水処理場に導き処理する下水道システムにおける、雨水滞水設備であって、
前記幹線流路からの越流水を取り込むための取水路と、
この取水路により取り込んだ越流水を固液分離する固液分離装置と、
この固液分離装置により分離された液分が供給される雨水滞水池とを備えており、
前記固液分離装置が、円筒型水槽と、円筒型水槽の内部に縦向きに配置された円筒型スクリーンとを備え、このスクリーンの接線方向に沿ってスクリーン内に越流水を送り込むことによりスクリーン内に渦流を発生させ、液分を前記スクリーンを通して水槽外に送り出す一方、固形分を水槽の中央下部に集め、この集めた固形分を水槽外に引抜くように構成した渦流式固液分離装置である、
ことを特徴とする下水道における雨水滞水設備。
The present invention that has solved the above-described problems and the effects thereof are as follows.
<Invention of Claim 1>
A stormwater stagnation facility in a sewer system that guides and treats sewage to a sewage treatment plant via a main channel,
An intake channel for taking in overflow water from the main channel,
A solid-liquid separation device for solid-liquid separation of overflow water taken in by this intake channel;
A rainwater pond that is supplied with the liquid separated by the solid-liquid separator, and
The solid-liquid separation device includes a cylindrical water tank and a cylindrical screen vertically disposed inside the cylindrical water tank, and the overflow liquid is fed into the screen along the tangential direction of the screen. Eddy current is generated, and the liquid component is sent out of the water tank through the screen. is there,
Rainwater stagnant equipment in sewers characterized by that.

(作用効果)
このように、取水した越流水を雨水滞水池に供給するに際し、渦流式固液分離装置を用いて固液分離することにより、供給効率を落とすことなく砂等の沈降性物質や夾雑物を効率良く除去できる。より詳細には、砂等の沈降性物質が沈降分離される(沈砂池に替わる効果)とともに、非沈降性の夾雑物は渦流の中心に引き寄せられることにより捕捉され分離される。よって、雨水滞水池内に流入する砂等や夾雑物を効果的に低減でき、清掃頻度の低減、維持管理の容易化を図ることができるようになる。
(Function and effect)
In this way, when the overflowed water is supplied to the rainwater reservoir, solid sediment is separated using a vortex-type solid-liquid separator so that sedimentary substances such as sand and impurities can be efficiently removed without reducing the supply efficiency. Can be removed well. More specifically, sedimentary substances such as sand are settled and separated (effect replacing the sedimentation basin), and non-sedimentable impurities are captured and separated by being drawn to the center of the vortex. Therefore, sand and other foreign substances flowing into the rainwater reservoir can be effectively reduced, and the frequency of cleaning can be reduced and maintenance can be facilitated.

<請求項2記載の発明>
前記渦流式固液分離装置により分離された固形分が供給される脱水機と、この脱水機により分離される固形分が供給される貯留部とを備え、貯留部に供給される固形分が前記幹線流路に戻されないように構成されている、請求項1記載の下水道における雨水滞水設備。
<Invention of Claim 2>
The dehydrator to which the solid content separated by the vortex-type solid-liquid separator is supplied, and the storage unit to which the solid content separated by the dehydrator is supplied, and the solid content supplied to the storage unit is The storm water stagnation facility in the sewer according to claim 1, wherein the facility is configured not to be returned to the main channel.

(作用効果)
渦流式固液分離装置により分離されるし渣(夾雑物)を主とする固形分は、幹線流路に戻して下水処理場での処理に任せるように構成することもできるが、捕集したし渣を幹線流路の下水に再分散し、下水処理場で再度捕集するのは非効率的である。しかし、渦流式固液分離装置により分離される固形分は、なお液分を多量に含むため、そのままでは貯留に向かない。
(Function and effect)
The solid content mainly composed of residue (contaminants) separated by the vortex type solid-liquid separation device can be returned to the main channel and left to the treatment at the sewage treatment plant, but collected. It is inefficient to re-disperse the residue in the sewage of the main channel and collect it again at the sewage treatment plant. However, since the solid content separated by the vortex type solid-liquid separation device still contains a large amount of liquid content, it is not suitable for storage as it is.

そこで、本項記載の発明では、渦流式固液分離装置により分離される固形分をさらに脱水機により脱水処理するとともに、この脱水処理により分離される固形分を貯留部に貯留し、幹線流路に戻さないように構成したものである。   Therefore, in the invention described in this section, the solid content separated by the vortex type solid-liquid separation device is further dehydrated by the dehydrator, and the solid content separated by this dehydration treatment is stored in the storage section, It is constituted so as not to return to.

<請求項3記載の発明>
前記越流水が通過されるスクリーンと、このスクリーンに捕捉された夾雑物を幹線流路に掻き落すスクレーパとが設けられた、請求項1または2記載の下水道における雨水滞水設備。
<Invention of Claim 3>
The rain water stagnation facility in the sewer system according to claim 1 or 2, further comprising a screen through which the overflow water passes and a scraper that scrapes off impurities trapped on the screen into the main channel.

(作用効果)
このようなスクリーン及びスクレーパを設けることにより、越流水に混じって粗大な夾雑物を取り込まずに済み、その後の固液分離処理の負荷を低減できるようになる。
(Function and effect)
By providing such a screen and a scraper, it is not necessary to take in coarse impurities mixed with overflow water, and the load of the subsequent solid-liquid separation process can be reduced.

<請求項4記載の発明>
前記渦流式固液分離装置に供給される越流水の濁度を計測する濁度計を備え、この濁度計により計測される濁度に応じた頻度で、前記水槽から固形分を間欠的に引抜くように構成した、請求項1〜3のいずれか1項に記載の下水道における雨水滞水設備。
<Invention of Claim 4>
A turbidimeter for measuring the turbidity of the overflow water supplied to the vortex solid-liquid separator is provided, and the solid content is intermittently removed from the water tank at a frequency according to the turbidity measured by the turbidimeter. The rainwater stagnation facility in the sewer according to any one of claims 1 to 3, wherein the facility is configured to be pulled out.

(作用効果)
このように、供給される越流水の濁度に応じた頻度で固形分を引き抜くように構成することにより、越流水の固形分含有量の変化に応じた固形分貯留量の変化を適切に捉え、分離能力の低下等の不具合の生じない適切な固形分貯留量に達した時点で、固形分の引き抜きを行うことができる。よって、適切かつ高効率で引き抜き作業がなされるようになる。
(Function and effect)
In this way, by configuring so that the solid content is extracted at a frequency according to the turbidity of the overflow water supplied, the change in the solid content storage amount corresponding to the change in the solid content content of the overflow water is properly captured. The solid content can be withdrawn when an appropriate solid content storage amount that does not cause problems such as a decrease in separation capacity is reached. Therefore, the drawing operation can be performed appropriately and with high efficiency.

<請求項5記載の発明>
前記渦流式固液分離装置の水槽内に残留する液分を、前記雨水滞水池に供給し洗浄するように構成した、請求項1〜4のいずれか1項に記載の下水道における雨水滞水設備。
<Invention of Claim 5>
The rainwater stagnant equipment in the sewer according to any one of claims 1 to 4, wherein liquid remaining in the water tank of the vortex solid-liquid separator is supplied to the rainwater catchment pond and washed. .

(作用効果)
このように、渦流式固液分離装置を雨水滞水池内をフラッシュ洗浄する手段として用いることにより、フラッシュゲートやフラッシュタンク等のフラッシュ洗浄設備を削減することが可能になる。
(Function and effect)
As described above, by using the vortex type solid-liquid separation device as a means for flushing the rainwater reservoir, it is possible to reduce flush washing facilities such as a flush gate and a flush tank.

<請求項6記載の発明>
下水を幹線流路を介して下水処理場に導き処理する下水道システムにおける、雨水滞水方法であって、
前記幹線流路から越流水を取り込み、取り込んだ越流水を円筒型水槽の内部に縦向きに配置された円筒型スクリーン内に、スクリーンの接線方向に沿って送り込み、スクリーン内に渦流を発生させ、液分を前記スクリーンを通して水槽外に送り出して雨水滞水池に供給する一方、固形分を水槽の中央下部に集め、この集めた固形分を水槽外に引抜くようにする、
ことを特徴とする下水道における雨水滞水方法。
<Invention of Claim 6>
In a sewer system that guides and treats sewage to a sewage treatment plant via a main channel,
The overflow water is taken in from the main channel, and the fetched overflow water is sent along the tangential direction of the screen into the cylindrical screen arranged vertically in the cylindrical water tank, and the vortex flow is generated in the screen. While sending the liquid component out of the water tank through the screen and supplying it to the rainwater reservoir, the solid content is collected at the bottom center of the water tank, and the collected solid content is drawn out of the water tank.
A method for stagnation of rainwater in a sewer.

(作用効果)
請求項1記載の発明と同様の作用効果が奏せられる。
(Function and effect)
The same effect as that of the first aspect of the invention can be achieved.

以上のとおり、本発明によれば、雨水滞水池における清掃頻度の低減、維持管理の容易化が図られる等の利点がもたらされる。   As described above, according to the present invention, there are advantages such as reduction in the frequency of cleaning in a rainwater reservoir and facilitation of maintenance and management.

図1は、合流式下水道における雨水滞水設備に本発明を適用した一実施形態を示している。すなわち、汚水及び雨水は共通の幹線流路1を介して下水処理場2に導かれる合流式下水道システムに対して、幹線流路1に越流堰3が設けられており、雨天時等において汚水及び雨水の供給量が所定量を超えると、この越流堰3からの越流水は取水路4を介して渦流式固液分離装置5に供給され、分離された液分が雨水滞水池6に供給され、一時的に貯留されるようになっている。雨水滞水池6は流出ゲート7及び流出管8を介して幹線流路1における越流堰3と下水処理設備2との間の部分に連通接続されており、必要に応じて、例えば雨が止む等により汚水及び雨水の供給量が所定量を下回るようになり、下水処理設備の処理量に余裕が生じると、流出ゲート7が開放され、雨水滞水池6の貯留水が下水処理場2に対して供給されるようになっている。下水処理場2で処理された処理水は放流路Yを経由して海や川等の公共用水域へ放流される。   FIG. 1 shows an embodiment in which the present invention is applied to a rainwater stagnant facility in a combined sewer. In other words, an overflow weir 3 is provided in the main channel 1 for the combined sewer system in which the sewage and rainwater are guided to the sewage treatment plant 2 through the common main channel 1, When the amount of rainwater supplied exceeds a predetermined amount, the overflow water from the overflow weir 3 is supplied to the vortex-type solid-liquid separator 5 via the intake channel 4 and the separated liquid is supplied to the rainwater catchment basin 6. Supplied and temporarily stored. The rainwater reservoir 6 is connected to a portion of the main channel 1 between the overflow weir 3 and the sewage treatment facility 2 via the outflow gate 7 and the outflow pipe 8, and for example, the rain stops when necessary. When the supply amount of sewage and rainwater falls below a predetermined amount due to the above, and there is room in the treatment amount of the sewage treatment facility, the outflow gate 7 is opened, and the stored water in the stormwater stagnation basin 6 is supplied to the sewage treatment plant 2. Are being supplied. The treated water treated in the sewage treatment plant 2 is discharged to a public water area such as the sea or a river through the discharge channel Y.

図2及び図3は、渦流式固液分離装置5の例を示している。この渦流式固液分離装置5は、円筒型水槽50と、円筒型水槽50の内部に縦向きに配置された円筒型スクリーン51とを備えている。また、被処理液を供給するための供給路52が水槽50の側部及びスクリーン51の側部を貫通しており、越流水をスクリーン51の接線方向に沿ってスクリーン51内に送り込むように構成されている。この被処理液の送り込みによりスクリーン51内に渦流が発生する。また、円筒型水槽50の側部には液分の排出路53が設けられ、中央下部には固形分の引抜き部50Dが設けられている。引抜き部50Dに対しては、外部に設置された引抜き弁5V及び引抜きポンプ5Pが連通接続され、これらにより引抜き制御がなされる。   2 and 3 show an example of the vortex type solid-liquid separator 5. The vortex type solid-liquid separation device 5 includes a cylindrical water tank 50 and a cylindrical screen 51 arranged vertically inside the cylindrical water tank 50. Further, the supply path 52 for supplying the liquid to be treated passes through the side of the water tank 50 and the side of the screen 51, and the overflow water is sent into the screen 51 along the tangential direction of the screen 51. Has been. A vortex flow is generated in the screen 51 by feeding the liquid to be processed. In addition, a liquid discharge path 53 is provided at the side of the cylindrical water tank 50, and a solid extraction part 50D is provided at the lower center. A drawing valve 5V and a drawing pump 5P installed outside are connected to the drawing portion 50D, and drawing control is performed by these.

このような円筒型スクリーン51を備える渦流式固液分離装置5では、円筒型スクリーン51を図4に示す形態、すなわちスクリーン51の目が、スクリーン51の内外方向で所定の角度を有するように設けられ、その目の円筒内側開口部Miがスクリーン51の内側Siの渦流Fiの流れ方向に逆らわない方向に向いており、円筒外側開口部Moはスクリーン51の内側Siの渦流Fiの流れ方向と反対の流れを生じさせるように向いている形態とするのが好ましい。さらに、図示のように、スクリーン51の渦流Fiに逆らうように向かっている面Aが円弧面に形成されているのが望ましい。かかるスクリーン51は、スクリーン51の外側Soに、内側Siに生ずる渦流Fiと、流れ方向が反対の流れFoが生じ、清澄水を効果的に槽外に送り出すことができるとともに、夾雑物がスクリーン51の目に引き込まれにくく目詰まりを起こし難いという特長がある。スクリーン51の目幅は適宜定めれば良いが、1.2〜5mmの範囲内で選択するのが好ましい。   In the vortex type solid-liquid separation device 5 having such a cylindrical screen 51, the cylindrical screen 51 is provided as shown in FIG. 4, that is, the eyes of the screen 51 have a predetermined angle in the inner and outer directions of the screen 51. The cylindrical inner opening Mi of the eye is directed in a direction that does not oppose the flow direction of the inner Si vortex flow Fi of the screen 51, and the cylindrical outer opening Mo is opposite to the flow direction of the inner Si vortex Fi of the screen 51. It is preferable to adopt a configuration that is suitable for generating the flow of Further, as shown in the drawing, it is desirable that the surface A facing the vortex flow Fi of the screen 51 is formed in an arc surface. In the screen 51, the vortex flow Fi generated in the inner Si and the flow Fo opposite in the flow direction are generated on the outer side So of the screen 51, and the clear water can be effectively sent out of the tank. There is a feature that it is hard to be drawn into the eyes and hardly clogs. The screen width of the screen 51 may be determined as appropriate, but is preferably selected within the range of 1.2 to 5 mm.

また、渦流式固液分離装置5は、雨水滞水池6とは別に設置しても良いが、図5及び図6に示すように雨水滞水池6と一体化し、雨水滞水池6の水面上のスペースに配置するのも好ましい形態である。   Further, the vortex type solid-liquid separation device 5 may be installed separately from the rainwater catchment basin 6, but is integrated with the rainwater catchment basin 6 as shown in FIGS. Arranging in a space is also a preferred form.

いずれにせよ、本実施形態の設備によれば、取水した越流水を雨水滞水池6に供給するのに先立ち、渦流式固液分離装置5を用いて固液分離することにより、供給効率を落とすことなく砂等の沈降性物質や夾雑物を効率良く除去できるようになり、処理量の低下なしに清掃頻度の低減、維持管理の容易化を図ることができるようになる。   In any case, according to the facility of the present embodiment, the supply efficiency is lowered by separating the collected overflow using the eddy current solid-liquid separation device 5 prior to supplying the overflow water to the rainwater reservoir 6. Accordingly, sedimentary substances such as sand and contaminants can be efficiently removed, and the frequency of cleaning can be reduced and maintenance can be facilitated without lowering the processing amount.

渦流式固液分離装置5からの固形分の引抜きは、定期的あるいは任意に行うこともできるが、越流水の固形分含有量に変動があるため適切な引抜きタイミングも変動する。よって、適切なタイミングで固形分を引抜くために、渦流式固液分離装置5の上流側に越流水の濁度を計測する濁度計9を設置し、この濁度計9により渦流式固液分離装置5に供給される越流水の濁度を計測し、この計測結果に応じた頻度で、固形分を間欠的に引抜くように構成するのは好ましい。具体的には、濁度と適切な引抜き時間間隔との関係を予め試験運転等により調べて一定のルールを定めておき、このルールに従って引抜き間隔を適切に変化させることができる。   The extraction of the solid content from the vortex solid-liquid separator 5 can be performed periodically or arbitrarily. However, since the solid content of the overflow water varies, the appropriate extraction timing also varies. Therefore, a turbidity meter 9 for measuring the turbidity of the overflow water is installed upstream of the vortex-type solid-liquid separator 5 in order to extract the solid content at an appropriate timing. It is preferable that the turbidity of the overflow water supplied to the liquid separator 5 is measured and the solid content is intermittently extracted at a frequency according to the measurement result. Specifically, a relationship between turbidity and an appropriate drawing time interval is examined in advance by a test operation or the like to determine a certain rule, and the drawing interval can be changed appropriately according to this rule.

一方、渦流式固液分離装置5により分離される固形分は、上記引抜きバルブ5V及び引抜きポンプ5Pにより、二点鎖線で示す流路Uを経て幹線流路1に戻し、下水処理場2での処理に任せるように構成することもできるが、前述のとおり非効率的である。よって、この分離固形分は脱水機10に供給し、脱水処理による減容化を図った後、この脱水処理により分離される固形分を貯留部11に貯留し、幹線流路1には戻さないようにするのも好ましい形態である。この脱水機10としてはスクリュープレス式、プレス式、ローラ式の脱水機等を好適に用いることができる。   On the other hand, the solid content separated by the vortex type solid-liquid separation device 5 is returned to the main channel 1 through the flow path U indicated by the two-dot chain line by the above-described extraction valve 5V and the extraction pump 5P. Although it can be configured to leave it to processing, it is inefficient as described above. Therefore, after this separated solid content is supplied to the dehydrator 10 and reduced in volume by the dehydration process, the solid content separated by this dehydration process is stored in the storage unit 11 and is not returned to the main channel 1. It is also a preferable form. As the dehydrator 10, a screw press type, a press type, a roller type dehydrator or the like can be suitably used.

この場合、脱水機10により分離される液分は、図中二点鎖線で示す流路Vを経て幹線流路1に戻すこともできるが、本来、雨水滞水池6に送られる液分であるから、流路12を介して雨水滞水池6に供給するように構成するのが好ましい。   In this case, the liquid component separated by the dehydrator 10 can be returned to the main channel 1 through the channel V indicated by the two-dot chain line in the figure, but is originally the component sent to the rainwater aquifer 6. Therefore, it is preferable that the rainwater catchment basin 6 is supplied via the flow path 12.

本発明では、図7に示すような通常の越流堰3、すなわち、幹線流路1を構成する溝状流路31と、取水路4を構成する溝状流路32とを並設し、これらの間に越流堰3を設けた通常の形態を採用することができる。しかし、この場合、粗大な夾雑物までもが越流水と伴に取り込まれ、渦流式固液分離装置5に供給されてしまい、目詰まりを起こす等の不具合を発生させるおそれがある。   In the present invention, a normal overflow weir 3 as shown in FIG. 7, that is, a groove-like flow passage 31 constituting the main passage 1 and a groove-like passage 32 constituting the intake channel 4 are arranged in parallel. The normal form which provided the overflow dam 3 between these can be employ | adopted. However, in this case, even coarse impurities are taken in along with the overflow water and are supplied to the vortex type solid-liquid separator 5, which may cause problems such as clogging.

よって、渦流式固液分離装置5の上流側に粗大な夾雑物を分離除去するための分離装置を設置するのは好ましい形態である。この場合、越流水は分離装置により粗大な夾雑物が分離除去された後、そのまま、すなわち凝集剤等の添加なく渦流式固液分離装置5に供給される。この分離装置としては、越流を妨げることなく効率良く粗大な夾雑物を除去できる点でスクリーンを用いた分離装置が好ましい。特に好ましいのは、図8及び図9に示すようなバースクリーン装置30である。このバースクリーン装置30では、所定の目幅間隔をもって支持された複数のバーからなるバースクリーン33と、各バー間を通り被処理液の供給側面に突出されたスクレーパ34と、このスクレーパ34をバーの長手方向に沿って移動させる図示しないシリンダ等の駆動装置とを備えているものである。バーの間隔は適宜定めれば良いが、5〜100mmの範囲内で選択するのが好ましい。またスクレーパ34はバーの長手方向に適宜の間隔をあけて複数箇所に設けるのが好ましい。   Therefore, it is a preferable embodiment to install a separation device for separating and removing coarse impurities on the upstream side of the vortex type solid-liquid separation device 5. In this case, the overflow water is supplied to the vortex solid-liquid separation device 5 as it is, that is, without adding a flocculant or the like after coarse impurities are separated and removed by the separation device. As this separation device, a separation device using a screen is preferable in that coarse impurities can be efficiently removed without hindering overflow. Particularly preferred is a bar screen device 30 as shown in FIGS. In this bar screen device 30, a bar screen 33 composed of a plurality of bars supported at a predetermined interval, a scraper 34 protruding between the bars and projecting to the supply side of the liquid to be treated, and the scraper 34 And a drive device such as a cylinder (not shown) that is moved along the longitudinal direction of the cylinder. The interval between the bars may be determined as appropriate, but is preferably selected within a range of 5 to 100 mm. The scrapers 34 are preferably provided at a plurality of positions with appropriate intervals in the longitudinal direction of the bar.

越流水はバースクリーン33のバー間を通過するが、粗大な夾雑物はバー間を通過できずに分離される。バー間に詰まる、引っ掛る等した夾雑物はスクレーパ34をバー長手方向に沿って移動することにより掻き落される。図示しないが、バースクリーン33の被処理液供給側に水位計を設置し、水位検知結果に応じて所定の水位になるとスクレーパ34を作動させるように構成することもできる。   Overflow water passes between the bars of the bar screen 33, but coarse impurities cannot pass between the bars and are separated. Contaminants such as clogged or caught between bars are scraped off by moving the scraper 34 along the longitudinal direction of the bar. Although not shown, it is also possible to install a water level meter on the liquid supply side of the bar screen 33 and operate the scraper 34 when a predetermined water level is reached according to the water level detection result.

この分離装置により分離した粗大な夾雑物は別途貯留しても良いが、設備の簡略化の観点から幹線流路1に戻すのが好ましい。したがってこの観点から、図10に示すように、上述のスクレーパ34を有するバースクリーン装置30を越流堰3に設け、越流水をバースクリーン33に通過させるように構成するのが好ましい。これにより、粗大な夾雑物はバースクリーン33を通過できず、スクレーパ34を作動させることによってスクリーン33に詰まる等した夾雑物は幹線流路1に戻されるようになる。   The coarse impurities separated by this separation device may be stored separately, but it is preferable to return to the main channel 1 from the viewpoint of simplification of equipment. Therefore, from this viewpoint, as shown in FIG. 10, it is preferable that the bar screen device 30 having the above-described scraper 34 is provided in the overflow weir 3 so that the overflow water passes through the bar screen 33. As a result, coarse impurities cannot pass through the bar screen 33, and by operating the scraper 34, foreign matters clogged in the screen 33 are returned to the main flow path 1.

越流堰3に対するバースクリーン装置30の設置姿勢は適宜定めることができ、図10に示すように越流堰3上にバースクリーン33を上下方向に沿って立設する形態の他、図11(a)に示すようにスクリーン33を水平に配置し、越流水をスクリーン33の上から下へ通過させる形態、図11(b)に示すようにスクリーン33を水平に配置し、越流水をスクリーン33の下から上へ通過させる形態、図示しないが、バーを上下方向に沿って延在させ、スクレーパを上下方向に移動させる形態等を採用することができる。   The installation posture of the bar screen device 30 with respect to the overflow weir 3 can be determined as appropriate. As shown in FIG. 10, the bar screen 33 is vertically provided on the overflow weir 3 along the vertical direction, as shown in FIG. As shown in FIG. 11A, the screen 33 is disposed horizontally and the overflow water is passed from the top to the bottom of the screen 33. The screen 33 is horizontally disposed as shown in FIG. Although not shown, a form in which the bar is extended in the vertical direction and a scraper is moved in the vertical direction can be employed.

他方、本発明では渦流式固液分離装置5を採用したことにより、悪臭やハエ発生の原因となる砂等の池内残留物が低減するが、完全に無くなるものではない。したがって、図1に示されるように、フラッシュゲート100及びフラッシュタンク101等のフラッシュ洗浄手段を設けることもできる。また一つの好ましい形態として、渦流式固液分離装置5の水槽内に残留する液分を利用して雨水滞水池6のフラッシュ洗浄をすることもできる。このために、渦流式固液分離装置5の水槽50から雨水滞水池6に通じる洗浄水供給路を設け、この洗浄水供給路にフラッシュバルブを設け、このフラッシュバルブは通常は閉じておき、必要に応じて開放することによりフラッシュ洗浄を行うように構成することができる。この場合、フラッシュゲート及びフラッシュタンク等のフラッシュ洗浄設備を一部または全部削減することができる。   On the other hand, in the present invention, the adoption of the vortex-type solid-liquid separation device 5 reduces the residue in the pond such as sand which causes bad odor and flies, but it is not completely eliminated. Therefore, as shown in FIG. 1, flash cleaning means such as a flash gate 100 and a flash tank 101 can be provided. Moreover, as one preferable form, the rain water reservoir 6 can be flushed using the liquid remaining in the water tank of the vortex solid-liquid separator 5. For this purpose, a washing water supply passage is provided from the water tank 50 of the vortex-type solid-liquid separator 5 to the rainwater reservoir 6 and a flush valve is provided in the washing water supply passage. This flush valve is normally closed and necessary. It can be configured to perform flash cleaning by opening it according to the above. In this case, flash cleaning equipment such as a flash gate and a flash tank can be partially or entirely reduced.

また、一般的な雨水滞水設備においては幹線流路1から取水した越流水の一部を雨水滞水池6に取り込み、残部をそのまま川や海などの公共用水域に放流することがあるが、本発明でもこれを採用でき、図1中にはこのための放流路Wが二点鎖線で示されている。   Moreover, in a general rainwater stagnant facility, a part of the overflow water taken from the main channel 1 may be taken into the rainwater stagnant pond 6 and the rest may be discharged directly into a public water area such as a river or the sea. This can also be adopted in the present invention. In FIG. 1, the discharge flow path W for this purpose is indicated by a two-dot chain line.

さらにまた、一般的な雨水滞水設備では、越流堰3の上流側の幹線流路1から汚水及び雨水を下水処理場2に直接供給する供給路を設けることがあるが、本発明でもこれを採用でき、図1中にはこの供給路Xが二点鎖線で示されている。   Furthermore, in a general rainwater stagnant facility, a supply path for supplying sewage and rainwater directly to the sewage treatment plant 2 from the main channel 1 upstream of the overflow weir 3 may be provided. In FIG. 1, this supply path X is indicated by a two-dot chain line.

本発明は、下水を幹線流路を介して下水処理場に導き処理する下水道システムにおける、雨水滞水設備に適用されるものである。すなわち、上記実施形態は、雨水と汚水とを同一の管渠で排除する合流式下水道を対象としたものであるが、本発明は、雨水と汚水とを個別の管渠で排除する分流式下水道システムにも適用できる。この場合、越流水に汚水が混じらないこと以外は、雨水を下水処理設備へ供給する幹線流路から越流水を取水し、渦流式固液分離装置を介して雨水滞水池に供給する基本部分を含め、応用例についても上記実施形態と基本的に同様であり、当業者であれば容易に理解できるため、敢えて説明を省略する。   The present invention is applied to a rainwater stagnant facility in a sewerage system that guides and treats sewage to a sewage treatment plant via a main channel. That is, the above embodiment is directed to a combined sewer that excludes rainwater and sewage with the same pipe, but the present invention is a separate sewer that excludes rainwater and sewage with separate pipes. It can also be applied to the system. In this case, except that sewage is not mixed with the overflow water, the basic part that takes the overflow water from the main channel that supplies rainwater to the sewage treatment facility and supplies it to the storm water reservoir through the vortex solid-liquid separator Including the application examples are basically the same as those in the above embodiment and can be easily understood by those skilled in the art.

また、越流水の取水形態としては、上記実施形態のように越流堰を設ける形態が一般的であるが、堰以外であっても、水位差を利用したオーバーフローにより取水するものであれば本発明を適用できる。   In addition, as the overflow water intake form, a form in which an overflow weir is provided as in the above embodiment is common, but even if it is other than the weir, if it is taken in by overflow using a water level difference, The invention can be applied.

さらに、一般的な雨水滞水設備の雨水滞水池6としては、上記例のように所定の貯留許容量まで貯留を行い、これを超える分についてはそのまま川や海などの公共用水域に放流する貯留型、オーバーフローにより下水処理場2に供給する沈殿型、原則としてオーバーフローにより下水処理場2に供給するが、雨水滞水池6に対する供給量が所定量を超えると超過分を放流する貯留/沈殿型があり、本発明はこれらのいずれにも適用できる。   Furthermore, as a rainwater catchment basin 6 of a general rainwater catchment facility, it stores up to a predetermined storage allowance as in the above example, and the excess is discharged as it is into a public water area such as a river or the sea. Storage type, sedimentation type that supplies to the sewage treatment plant 2 by overflow, in principle, storage type / sedimentation type that supplies to the sewage treatment plant 2 by overflow, but discharges the excess when the supply amount to the rainwater reservoir 6 exceeds a predetermined amount The present invention can be applied to any of these.

さらにまた、図1に示す形態は自然流下により供給される雨水・汚水を雨水滞水池6に貯留する自然流下形態への適用例であるが、図12に示すように、越流水を沈砂池102に貯留して砂等の沈降物質を除去した後、雨水ポンプ103により雨水滞水池6に供給するポンプ場放流形態にも適用できる。このポンプ場放流形態では、沈砂池102で除去されない砂等が、雨水滞水池6への供給に先立って渦流式固液分離装置5により補完的に除去されることになる。これに対して、前者の自然流下形態における渦流式固液分離装置5は、沈砂池102の分まで砂等を除去する役割を担うことになる。   Furthermore, although the form shown in FIG. 1 is an example of application to a natural flow form in which rainwater / sewage supplied by natural flow is stored in the storm water reservoir 6, as shown in FIG. It can also be applied to a pumping station discharge form in which it is stored in the tank and sedimentary substances such as sand are removed and then supplied to the storm water reservoir 6 by the rainwater pump 103. In this pump station discharge form, sand and the like that are not removed by the sand basin 102 are complementarily removed by the vortex-type solid-liquid separator 5 prior to the supply to the storm water reservoir 6. On the other hand, the former eddy current type solid-liquid separation device 5 in the natural flow mode plays a role of removing sand and the like up to the sand basin 102.

本実施の形態にかかる越流水の処理方法の概略を示すフロー図である。It is a flowchart which shows the outline of the processing method of the overflow water concerning this Embodiment. 渦流式固液分離装置の概略を示す斜視図である。It is a perspective view which shows the outline of an eddy current type solid-liquid separator. 図2のIII−III断面図である。FIG. 3 is a sectional view taken along line III-III in FIG. 2. スクリーンの要部拡大断面図である。It is a principal part expanded sectional view of a screen. 雨水滞水池の一形態を概略的に示す縦断面図である。It is a longitudinal cross-sectional view which shows schematically one form of a rainwater reservoir. 雨水滞水池の一形態を概略的に示す横断面図である。It is a cross-sectional view which shows schematically one form of a rainwater reservoir. 越流堰の一形態を示す斜視図である。It is a perspective view which shows one form of an overflow dam. バースクリーン装置を概略的に示す正面図である。It is a front view which shows a bar screen apparatus schematically. バースクリーン装置を概略的に示す横断面図である。It is a cross-sectional view which shows a bar screen apparatus schematically. 越流堰の好適な形態を示す斜視図である。It is a perspective view which shows the suitable form of an overflow dam. バースクリーン装置の各種設置形態を示す概略図である。It is the schematic which shows the various installation forms of a bar screen apparatus. 対象となる雨水滞水設備の例を示すフロー図である。It is a flowchart which shows the example of the rainwater stagnant water equipment used as object.

符号の説明Explanation of symbols

1…幹線流路、2…下水処理場、3…越流堰、4…取水路、5…渦流式固液分離装置、6…雨水滞水池。   DESCRIPTION OF SYMBOLS 1 ... Main line flow path, 2 ... Sewage treatment plant, 3 ... Overflow weir, 4 ... Intake channel, 5 ... Eddy current type solid-liquid separator, 6 ... Rainwater stagnation pond.

Claims (6)

下水を幹線流路を介して下水処理場に導き処理する下水道システムにおける、雨水滞水設備であって、
前記幹線流路からの越流水を取り込むための取水路と、
この取水路により取り込んだ越流水を固液分離する固液分離装置と、
この固液分離装置により分離された液分が供給される雨水滞水池とを備えており、
前記固液分離装置が、円筒型水槽と、円筒型水槽の内部に縦向きに配置された円筒型スクリーンとを備え、このスクリーンの接線方向に沿ってスクリーン内に越流水を送り込むことによりスクリーン内に渦流を発生させ、液分を前記スクリーンを通して水槽外に送り出す一方、固形分を水槽の中央下部に集め、この集めた固形分を水槽外に引抜くように構成した渦流式固液分離装置である、
ことを特徴とする下水道における雨水滞水設備。
A stormwater stagnation facility in a sewer system that guides and treats sewage to a sewage treatment plant via a main channel,
An intake channel for taking in overflow water from the main channel,
A solid-liquid separation device for solid-liquid separation of overflow water taken in by this intake channel;
A rainwater pond that is supplied with the liquid separated by the solid-liquid separator, and
The solid-liquid separation device includes a cylindrical water tank and a cylindrical screen vertically disposed inside the cylindrical water tank, and the overflow liquid is fed into the screen along the tangential direction of the screen. A vortex type solid-liquid separation device configured to collect the solid content at the center lower part of the water tank and draw out the collected solid content outside the water tank. is there,
Rainwater stagnant equipment in sewers characterized by that.
前記渦流式固液分離装置により分離された固形分が供給される脱水機と、この脱水機により分離される固形分が供給される貯留部とを備え、貯留部に供給される固形分が前記幹線流路に戻されないように構成されている、請求項1記載の下水道における雨水滞水設備。   The dehydrator to which the solid content separated by the vortex-type solid-liquid separator is supplied, and the storage unit to which the solid content separated by the dehydrator is supplied, and the solid content supplied to the storage unit is The storm water stagnation facility in the sewer according to claim 1, wherein the facility is configured not to be returned to the main channel. 前記越流水が通過されるスクリーンと、このスクリーンに捕捉された夾雑物を幹線流路に掻き落すスクレーパとが設けられた、請求項1または2記載の下水道における雨水滞水設備。   The rain water stagnation facility in the sewer system according to claim 1 or 2, further comprising a screen through which the overflow water passes and a scraper that scrapes off impurities trapped on the screen into the main channel. 前記渦流式固液分離装置に供給される越流水の濁度を計測する濁度計を備え、この濁度計により計測される濁度に応じた頻度で、前記水槽から固形分を間欠的に引抜くように構成した、請求項1〜3のいずれか1項に記載の下水道における雨水滞水設備。   A turbidimeter for measuring the turbidity of the overflow water supplied to the vortex solid-liquid separator is provided, and the solid content is intermittently removed from the water tank at a frequency according to the turbidity measured by the turbidimeter. The rainwater stagnation facility in the sewer according to any one of claims 1 to 3, wherein the facility is configured to be pulled out. 前記渦流式固液分離装置の水槽内に残留する液分を、前記雨水滞水池に供給し洗浄するように構成した、請求項1〜4のいずれか1項に記載の下水道における雨水滞水設備。   The rainwater stagnant equipment in the sewer according to any one of claims 1 to 4, wherein liquid remaining in the water tank of the vortex solid-liquid separator is supplied to the rainwater catchment pond and washed. . 下水を幹線流路を介して下水処理場に導き処理する下水道システムにおける、雨水滞水方法であって、
前記幹線流路から越流水を取り込み、取り込んだ越流水を円筒型水槽の内部に縦向きに配置された円筒型スクリーン内に、スクリーンの接線方向に沿って送り込み、スクリーン内に渦流を発生させ、液分を前記スクリーンを通して水槽外に送り出して雨水滞水池に供給する一方、固形分を水槽の中央下部に集め、この集めた固形分を水槽外に引抜くようにする、
ことを特徴とする下水道における雨水滞水方法。
In a sewer system that guides and treats sewage to a sewage treatment plant via a main channel,
The overflow water is taken in from the main channel, and the fetched overflow water is sent along the tangential direction of the screen into the cylindrical screen arranged vertically in the cylindrical water tank, and the vortex flow is generated in the screen. While sending the liquid component out of the water tank through the screen and supplying it to the rainwater reservoir, the solid content is collected at the bottom center of the water tank, and the collected solid content is drawn out of the water tank.
A method for stagnation of rainwater in a sewer.
JP2004219000A 2004-07-27 2004-07-27 Rainwater reservoir facility in sewerage and its method Pending JP2006037510A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004219000A JP2006037510A (en) 2004-07-27 2004-07-27 Rainwater reservoir facility in sewerage and its method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publications (1)

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Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007016582A (en) * 2005-06-08 2007-01-25 Sekisui Chem Co Ltd Drain channel structure suppressing flow out of rain water
CN108487439A (en) * 2018-05-24 2018-09-04 深圳市创环环保科技有限公司 A kind of water outlet mosquito proof mechanism and section dirty formula environmentally-friendly gutter inlet device
CN114086582A (en) * 2021-11-29 2022-02-25 山东安澜工程建设有限公司 Energy-concerving and environment-protective type's water conservancy construction equipment

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007016582A (en) * 2005-06-08 2007-01-25 Sekisui Chem Co Ltd Drain channel structure suppressing flow out of rain water
CN108487439A (en) * 2018-05-24 2018-09-04 深圳市创环环保科技有限公司 A kind of water outlet mosquito proof mechanism and section dirty formula environmentally-friendly gutter inlet device
CN114086582A (en) * 2021-11-29 2022-02-25 山东安澜工程建设有限公司 Energy-concerving and environment-protective type's water conservancy construction equipment
CN114086582B (en) * 2021-11-29 2023-02-07 山东安澜工程建设有限公司 Energy-concerving and environment-protective type's water conservancy construction equipment

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