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JP5926663B2 - In-pipe purification equipment - Google Patents

In-pipe purification equipment Download PDF

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JP5926663B2
JP5926663B2 JP2012211113A JP2012211113A JP5926663B2 JP 5926663 B2 JP5926663 B2 JP 5926663B2 JP 2012211113 A JP2012211113 A JP 2012211113A JP 2012211113 A JP2012211113 A JP 2012211113A JP 5926663 B2 JP5926663 B2 JP 5926663B2
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tube
solid
pipe
sewage
liquid separation
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JP2014066044A (en
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善治 松原
善治 松原
松坂 勝雄
勝雄 松坂
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Sekisui Chemical Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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    • Y02W10/10Biological treatment of water, waste water, or sewage

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Description

本発明は、汚水中の固形物による目詰まりを防止し、安定的に汚水を処理できる管路内浄化装置に関する。 The present invention relates to an in-pipe purification apparatus that prevents clogging with solid matter in sewage and can stably treat sewage.

近年、下水処理施設の負担を軽減するために、微生物を用いて管路内で汚水を浄化する方法が提案されている。
例えば、特許文献1には、管路内に、微生物が定着可能な通水性の固定床と、固定床中に酸素を供給するための酸素供給手段を有することにより、固定床が汚水中に浸漬した状態であっても、固定床中に酸素を供給し、好気性微生物の増殖を促進できる管路用浄水装置が開示されている。
また、特許文献2には、圧送管の管路の内側にフィンを設け、圧送管内部に複数のパイプを設置することにより、汚水と微生物とが接触する面積を拡大させ、効率的に汚水を浄化する方法が開示されている。
In recent years, in order to reduce the burden on a sewage treatment facility, a method for purifying sewage in a pipeline using microorganisms has been proposed.
For example, Patent Document 1 discloses that a fixed bed is immersed in sewage by having a water-permeable fixed bed capable of fixing microorganisms and an oxygen supply means for supplying oxygen into the fixed bed. Even in such a state, a water purifier for a pipeline that can supply oxygen into a fixed bed and promote the growth of aerobic microorganisms has been disclosed.
Further, in Patent Document 2, fins are provided on the inside of the pipeline of the pressure feeding pipe, and a plurality of pipes are installed inside the pressure feeding pipe, thereby expanding the area where the sewage and the microorganisms come into contact with each other, and efficiently collecting the sewage. A method of purification is disclosed.

しかしながら、特許文献1や特許文献2に開示された方法では、汚水を長期間流した場合に、固定床やフィンの生物膜に汚水中の固形物や繊維分が付着して目詰まりをおこし、微生物と汚水の接触効率が低下するため、汚水の浄化性能が悪化することがあった。即ち、従来の管路内に多量の微生物を保持し、効率的に微生物に酸素を供給する手段を有する管路内浄化装置は、固形物による目詰まりが生じやすいという問題があった。 However, in the methods disclosed in Patent Document 1 and Patent Document 2, when sewage is run for a long period of time, solid matter and fibers in the sewage adhere to the fixed bed or fin biofilm, causing clogging. Since the contact efficiency of sewage is reduced, the purification performance of sewage may be deteriorated. That is, the conventional in-pipe purification apparatus having a means for holding a large amount of microorganisms in the pipe line and efficiently supplying oxygen to the microorganisms has a problem that clogging with solid substances is likely to occur.

特開2010−024773号公報JP 2010-024773 A 実開平6−24799号公報Japanese Utility Model Publication No. 6-24799

下水道施設計画・設計指針と解説(後編)−2009年版−P71 社団法人 日本下水道協会 平成21年9月発行Sewerage Facility Planning and Design Guidelines and Explanation (Part 2) -2009 Edition-P71 Japan Sewerage Association issued in September 2009

本発明は、汚水中の固形物による目詰まりを防止し、安定的に汚水を処理できる管路内浄化装置を提供することを目的とする。 An object of this invention is to provide the purification apparatus in a pipe line which can prevent clogging with the solid substance in wastewater, and can process wastewater stably.

本発明は、汚水を生物膜で処理する生物膜処理管と、該生物膜処理管へ汚水を供給する前に汚水を固液分離する固液分離管とを備え、上記生物膜処理管は、汚水による濾材の浸漬と空気による濾材の曝露とを間欠的に繰り返す構造を有するとともに、上記固液分離管内の汚水の水位が上がり溢流することで上澄水が上記生物膜処理管に供給される管路内浄化装置である。
以下に本発明を詳述する。
The present invention comprises a biofilm treatment tube for treating sewage with a biofilm, and a solid-liquid separation tube for solid-liquid separation of sewage before supplying the sewage to the biofilm treatment tube, together with the intermittently repeated structure and a filter media exposure by immersion and air filter medium by sewage, upper supernatant water is Ru is supplied to the biofilm process tube by overflowing up water level in the sewage above the solid-liquid separation tube In-pipe purification device.
The present invention is described in detail below.

本発明者らは、汚水中の固形物が生物膜に付着すること等による目詰まりを防止するために、微生物と接触させる前に予め汚水から固形物を分離しておくことを考えた。しかしながら、非特許文献1に開示されているような従来の沈殿分離槽では、管路内浄化装置の一部として地下に埋設することが困難であり、実用的でない。
そこで本発明者らは、汚水を生物膜で処理する生物膜処理管に、汚水を固液分離するための固液分離管を接続し、該固液分離管により固形物を分離してから該生物膜処理管へ汚水を供給することにより、該生物膜処理管が、管路内に多量の微生物を保持し、効率的に微生物に酸素を供給する手段を有するものであっても、汚水中の固形物による目詰まりを防止し、安定的に汚水を処理できることを見出し、本発明を完成させるに至った。
In order to prevent clogging due to the solid matter in the sewage adhering to the biofilm, the present inventors considered to separate the solid matter from the sewage before contacting with microorganisms. However, in the conventional sedimentation separation tank as disclosed in Non-Patent Document 1, it is difficult to embed in the underground as a part of the in-pipe purification device, which is not practical.
Therefore, the present inventors connect a solid-liquid separation tube for solid-liquid separation of sewage to a biofilm treatment tube for treating sewage with a biofilm, and after separating solids with the solid-liquid separation tube, By supplying sewage to the biofilm treatment tube, even if the biofilm treatment tube has a means for holding a large amount of microorganisms in the pipeline and efficiently supplying oxygen to the microorganisms, The present inventors have found that clogging due to solid matter can be prevented and that sewage can be treated stably, and the present invention has been completed.

本発明の管路内浄化装置は、生物膜処理管へ汚水を供給する前に汚水を固液分離する固液分離管を有する。上記固液分離管を有することにより、本発明の管路内浄化装置は、汚水中の固形物が微生物膜に付着すること等による目詰まりを防止し、長期間に亘って安定的な処理性能を維持できる。 The in-pipe purification apparatus of the present invention has a solid-liquid separation pipe that separates sewage into solid-liquid before supplying the sewage to the biofilm treatment pipe. By having the solid-liquid separation pipe, the in-pipe purification apparatus of the present invention prevents clogging due to the solid matter in the sewage adhering to the microbial membrane, and stable processing performance over a long period of time. Can be maintained.

上記固液分離管により汚水を固液分離する方法としては、例えば、沈殿分離、浮上分離、機械式スクリーン等の方法が挙げられる。なかでも、固液分離管の製造が低コストでできることから、沈殿分離による方法が好ましい。 Examples of the method for solid-liquid separation of sewage using the solid-liquid separation tube include methods such as precipitation separation, floating separation, and mechanical screen. Among these, the method by precipitation separation is preferable because the production of the solid-liquid separation tube can be performed at low cost.

上記固液分離管の流路方向の長さは、4m以上であることが好ましい。上記固液分離管の流路方向の長さが4m未満であると、汚水中の固形物を充分に分離できないことがある。 The length of the solid-liquid separation tube in the flow path direction is preferably 4 m or more. If the length of the solid-liquid separation tube in the flow path direction is less than 4 m, the solid matter in the sewage may not be sufficiently separated.

上記固液分離管の内径の好ましい下限は1.0m、好ましい上限は3.5mである。上記固液分離管の内径が1.0m未満であると、汚水中の固形物を充分に分離できなかったり、分離した固形物によって固液分離管が詰まったりすることがある。上記固液分離管の内径が3.5mを超えると、地下に埋設することが困難になったり、道路を通行するのに許可が必要になったりする。上記固液分離管の内径のより好ましい下限は2.0m、より好ましい上限は3.0mである。 The preferable lower limit of the inner diameter of the solid-liquid separation tube is 1.0 m, and the preferable upper limit is 3.5 m. If the inner diameter of the solid-liquid separation tube is less than 1.0 m, the solid matter in the sewage may not be sufficiently separated, or the solid-liquid separation tube may be clogged with the separated solid matter. If the inner diameter of the solid-liquid separation tube exceeds 3.5 m, it will be difficult to embed it underground, or permission will be required to travel on the road. The more preferable lower limit of the inner diameter of the solid-liquid separation tube is 2.0 m, and the more preferable upper limit is 3.0 m.

上記固液分離管には、通常、固液分離管へ汚水を流入する汚水流入管と、固液分離管から生物膜処理管へ汚水を流出する汚水流出管とが接続される。
沈殿分離により汚水を固液分離する場合、上記固液分離管の内径は、上記汚水流入管の内径の5倍以上であることが好ましい。上記固液分離管の内径が上記汚水流入管の内径の5倍未満であると、固液分離管内を流れる汚水の流速が速くなり、汚水中の固形物を充分に沈殿分離できないことがある。上記固液分離管の内径は、上記汚水流入管の内径の10倍以上であることがより好ましい。
上記固液分離管の内径は、上記汚水流入管の内径よりも大きければ大きいほど、固液分離管内を流れる汚水の流速が低下して沈殿分離による固液分離性能が向上するが、地下に埋設する場合の埋設の容易性の観点から、上記汚水流入管の内径の20倍以下であることが好ましい。
The solid-liquid separation pipe is usually connected to a sewage inflow pipe for flowing sewage into the solid-liquid separation pipe and a sewage outflow pipe for flowing sewage from the solid-liquid separation pipe to the biofilm treatment pipe.
When solid-liquid separation of sewage is performed by precipitation separation, the inner diameter of the solid-liquid separation pipe is preferably at least 5 times the inner diameter of the sewage inflow pipe. If the inner diameter of the solid-liquid separation pipe is less than five times the inner diameter of the sewage inflow pipe, the flow rate of sewage flowing through the solid-liquid separation pipe increases, and solid matter in the sewage may not be sufficiently separated by precipitation. The inner diameter of the solid-liquid separation pipe is more preferably 10 times or more the inner diameter of the sewage inflow pipe.
The larger the inner diameter of the solid-liquid separation pipe, the larger the inner diameter of the sewage inflow pipe, the lower the flow rate of the sewage flowing through the solid-liquid separation pipe, and the solid-liquid separation performance by precipitation separation is improved. From the viewpoint of ease of embedding, the inner diameter of the sewage inflow pipe is preferably 20 times or less.

沈殿分離により汚水を固液分離する場合、上記固液分離管は、上記固液分離管内を流れる汚水の水位が固液分離管の底部から1m以上高くなった際に汚水の上澄水を生物膜処理管へ排出する構造を有することが好ましい。固液分離管内を流れる汚水の水位が1m未満であると、汚水中の固形物を充分に分離できないことがある。固液分離管内を流れる汚水の水位は、1.5m以上であることがより好ましい。
固液分離管内を流れる汚水の水位は、高ければ高いほど、固液分離性能が向上するが、固液分離管内を流れる汚水の水位が高くなるようにするには固液分離管の内径を大きくする必要があり、地下に埋設する場合の埋設の容易性の観点から、4m以下であることが好ましい。
When the sewage is separated into solid and liquid by precipitation separation, the solid-liquid separation tube is used to remove the supernatant water from the sewage when the water level of the sewage flowing through the solid-liquid separation tube is higher than 1 m from the bottom of the solid-liquid separation tube. It is preferable to have a structure for discharging to the processing tube. If the level of the sewage flowing through the solid-liquid separation tube is less than 1 m, solids in the sewage may not be sufficiently separated. The level of sewage flowing through the solid-liquid separation tube is more preferably 1.5 m or more.
The higher the level of sewage flowing in the solid-liquid separation pipe, the better the solid-liquid separation performance.In order to increase the level of sewage flowing in the solid-liquid separation pipe, the inner diameter of the solid-liquid separation pipe must be increased. From the viewpoint of ease of embedding in the case of embedding underground, it is preferably 4 m or less.

上記汚水流出管により、固液分離管から生物膜処理管へ汚水を排出する方法としては、例えば、固液分離管内において、汚水の上澄水を生物膜処理管へ排出する際の汚水の水位として設定する高さに対応する位置に越流堰を設けておき、固液分離管内を流れる汚水の水位が該越流堰よりも高くなった時に、上澄水が越流堰から溢流して汚水流出管へ流れ込むようにする方法等が挙げられる。 As a method of discharging sewage from the solid-liquid separation pipe to the biofilm treatment pipe by the above sewage outflow pipe, for example, in the solid-liquid separation pipe, An overflow weir is installed at a position corresponding to the set height, and when the level of sewage flowing in the solid-liquid separation pipe becomes higher than the overflow weir, the supernatant water overflows from the overflow weir and the sewage flows out. The method etc. which make it flow into a pipe | tube are mentioned.

上記固液分離管は、固液分離性能の観点から、流入汚水量に対して、固液分離管の水面積に対する水面積負荷が70m/m・日以下であることが好ましく、有効貯留容積に対する滞留時間は1.5時間以上であることが好ましく、上記越流堰を設ける場合、越流堰の長さに対する越流堰負荷が150m/m・日以下であることが好ましい。 From the viewpoint of solid-liquid separation performance, the solid-liquid separation pipe preferably has a water area load of 70 m 3 / m 2 · day or less with respect to the water area of the solid-liquid separation pipe with respect to the amount of incoming sewage. The residence time with respect to the volume is preferably 1.5 hours or longer. When the overflow weir is provided, the overflow weir load with respect to the length of the overflow weir is preferably 150 m 3 / m · day or less.

上記固液分離管の材質は、汚水に対して耐久性を有するものであれば特に限定されないが、例えば、ポリエチレン、塩化ビニル等の樹脂や、鉄、ダクタイル鋳鉄等の金属や、繊維強化プラスチックスや、鉄筋コンクリート(ヒューム管)等が挙げられる。 The material of the solid-liquid separation tube is not particularly limited as long as it has durability against sewage. For example, resins such as polyethylene and vinyl chloride, metals such as iron and ductile cast iron, and fiber reinforced plastics are used. And reinforced concrete (fume pipe).

上記固液分離管は、汚水から分離した後の固形物を容易に除去できる構造を有していることが好ましい。具体的には例えば、バキュームカー等で固形物を引き抜き廃棄するための固形物排出口を固液分離管に設けておくこと等が挙げられる。 It is preferable that the solid-liquid separation tube has a structure that can easily remove solids after being separated from sewage. Specifically, for example, a solid matter discharge port for drawing and discarding solid matter with a vacuum car or the like is provided in the solid-liquid separation tube.

本発明の管路内浄化装置は、汚水を生物膜で処理する生物膜処理管を有する。上記固液分離管を有することによる目詰まりを防止する効果は、生物膜処理管が多量の微生物を保持し、効率的に微生物に酸素を供給する手段を有する場合に特に大きく発揮される。多量の微生物を保持する生物膜処理管としては、具体的には、生物膜の表面積が管路内面の表面積に対して10倍以上であるものが挙げられる。 The in-pipe purification apparatus of the present invention has a biofilm treatment tube for treating sewage with a biofilm. The effect of preventing clogging by having the solid-liquid separation tube is particularly significant when the biofilm treatment tube holds a large amount of microorganisms and has means for efficiently supplying oxygen to the microorganisms. Specific examples of the biofilm treatment tube holding a large amount of microorganisms include those having a surface area of the biofilm that is 10 times or more the surface area of the inner surface of the pipe.

多量の微生物を保持し、効率的に微生物に酸素を供給する手段を有する生物膜処理管としては、汚水による濾材の浸漬と空気による濾材の曝露とを間欠的に繰り返す構造を有する生物膜処理管が好ましく、外管と、透水性を有する内管とからなる二重管の外管と内管との間隙に微生物を坦持した担体(微生物担体)が充填されている構造を有する生物膜処理管がより好ましい。
上記内管に透水性を付与する手段としては、例えば、内管に開口部を設ける方法等が挙げられる。上記内管に長期間汚水を流すと、開口部に汚水中の固形分が付着、蓄積し、目詰まりが生じることがある。また、開口部の目詰まりを防止するために開口部の目開きを大きくすると、外管と内管との間隙に充填した微生物担体に固形物が付着、蓄積し、微生物担体が目詰まりを起こすことがある。
従って、このような生物膜処理管に固液分離管を接続し、予め汚水中の固形物を分離しておくことにより、濾材や微生物担体の目詰まりを防止することができ、長期間に亘って安定的な処理性能が維持できる。また、固形物が分離除去された後の汚水を、生物膜処理管で処理するため、管路内浄化装置全体の処理性能が向上する。
As a biofilm treatment tube having a means for holding a large amount of microorganisms and efficiently supplying oxygen to the microorganisms, a biofilm treatment tube having a structure that intermittently repeats immersion of the filter medium with sewage and exposure of the filter medium with air Biofilm treatment having a structure in which a carrier (microorganism carrier) carrying microorganisms is filled in the gap between the outer tube and the inner tube of a double tube comprising an outer tube and a water-permeable inner tube A tube is more preferred.
Examples of means for imparting water permeability to the inner tube include a method of providing an opening in the inner tube. If sewage is allowed to flow through the inner pipe for a long period of time, solid matter in the sewage may adhere to and accumulate in the opening, resulting in clogging. In addition, if the opening of the opening is enlarged to prevent clogging of the opening, solid matter adheres and accumulates on the microbial carrier filled in the gap between the outer tube and the inner tube, and the microbial carrier is clogged. Sometimes.
Therefore, by connecting a solid-liquid separation tube to such a biofilm treatment tube and separating the solid matter in the sewage in advance, clogging of the filter medium and microbial carrier can be prevented, and for a long period of time. And stable processing performance can be maintained. Moreover, since the sewage after the solid matter is separated and removed is treated with the biofilm treatment tube, the treatment performance of the entire in-pipe purification device is improved.

上記生物膜処理管及び上記固液分離管は、管状であることにより、地下に埋設したり、必要に応じて上記生物膜処理管及び上記固液分離管のそれぞれの管路を延長したりすることが容易となる。
上記生物膜処理管及び上記固液分離管は、管路径方向の断面形状が矩形であってもよいし円形であってもよいが、円形であることが好ましい。
Since the biofilm treatment tube and the solid-liquid separation tube are tubular, they are buried underground, or the respective pipe lines of the biofilm treatment tube and the solid-liquid separation tube are extended as necessary. It becomes easy.
The biofilm treatment tube and the solid-liquid separation tube may have a circular or circular cross-sectional shape, but are preferably circular.

本発明によれば、汚水中の固形物による目詰まりを防止し、安定的に汚水を処理できる管路内浄化装置を提供することができる。 ADVANTAGE OF THE INVENTION According to this invention, the clogging by the solid substance in wastewater can be prevented, and the in-pipe purification apparatus which can process a wastewater stably can be provided.

図1は、本発明の管路内浄化装置の一例を示す長手方向(流路方向)の断面図である。FIG. 1 is a cross-sectional view in the longitudinal direction (flow path direction) showing an example of the in-pipe purification apparatus of the present invention. 図2は、図1に示した固液分離管の管路径方向の断面図である。FIG. 2 is a cross-sectional view of the solid-liquid separation pipe shown in FIG. 1 in the pipe radial direction.

以下に図面を用いて本発明の汚水処理装置を更に詳しく説明するが、本発明は、これら図面に示した実施形態のみに限定されない。 Hereinafter, the sewage treatment apparatus of the present invention will be described in more detail with reference to the drawings. However, the present invention is not limited only to the embodiments shown in these drawings.

図1は、本発明の管路内浄化装置の一例を示す長手方向(流路方向)の断面図であり、図2は、図1に示した固液分離管の管路径方向の断面図である。
図1の管路内浄化装置1は、汚水を生物膜で処理する生物膜処理管2と、該生物膜処理管へ汚水を供給する前に汚水を固液分離する固液分離管3とを有する。図1に示した固液分離管3は、沈殿分離により汚水を固液分離するものである。固液分離管3には、固液分離管3へ汚水6を流入する汚水流入管4と、固液分離管3から生物膜処理管2へ汚水6を流出する汚水流出管5とが接続されている。
1 is a cross-sectional view in the longitudinal direction (flow path direction) showing an example of the in-pipe purification apparatus of the present invention, and FIG. 2 is a cross-sectional view in the pipe radial direction of the solid-liquid separation pipe shown in FIG. is there.
The in-pipe purification apparatus 1 in FIG. 1 includes a biofilm treatment tube 2 that treats sewage with a biofilm, and a solid-liquid separation tube 3 that separates sewage into solid and liquid before supplying the sewage to the biofilm treatment tube. Have. The solid-liquid separation tube 3 shown in FIG. 1 separates sewage into solid and liquid by precipitation separation. Connected to the solid-liquid separation tube 3 are a sewage inflow tube 4 for flowing the sewage 6 into the solid-liquid separation tube 3 and a sewage outflow tube 5 for flowing the sewage 6 from the solid-liquid separation tube 3 into the biofilm treatment tube 2. ing.

汚水流入管4を流れる汚水6は、内径の大きい固液分離管3に流入すると、流速が著しく低下し、汚水6中の固形物7は固液分離管3の底部に沈殿する。
図2に示したように、固液分離管3には越流堰8が設けられている。汚水6から固形物7と分離された上澄水9は、固液分離管3内の汚水6の水位が上がることで越流堰8から溢流して汚水流出管5へ流入し、そのまま生物膜処理管2へ供給される。生物膜処理管2に供給された上澄水9は、生物膜処理管2内で浄化処理される。
When the sewage 6 flowing through the sewage inflow pipe 4 flows into the solid-liquid separation pipe 3 having a large inner diameter, the flow velocity is remarkably reduced, and the solid matter 7 in the sewage 6 is precipitated at the bottom of the solid-liquid separation pipe 3.
As shown in FIG. 2, an overflow weir 8 is provided in the solid-liquid separation pipe 3. The supernatant water 9 separated from the solid matter 7 from the sewage 6 overflows from the overflow weir 8 due to the rise of the level of the sewage 6 in the solid-liquid separation pipe 3 and flows into the sewage outflow pipe 5 as it is. Supplied to the tube 2. The supernatant water 9 supplied to the biofilm treatment tube 2 is purified in the biofilm treatment tube 2.

汚水6中の固形物7は、固液分離管3で分離されているため生物膜処理管2へ流出せず、上澄水9のみが生物膜処理管2へ供給される。そのため、生物膜処理管2の生物膜に固形物7が付着したり、生物膜処理管2が、図1に示したような、外管10と、透水性を有する内管11とからなる二重管構造である場合に内管11の開口部や内管11と外管10との間隙に充填した微生物担体12に固形物7が詰まったりすることが防止される。
なお、図1では、生物膜処理管2として、二重管構造を有する生物膜処理管を記載しているが、本発明の管路内浄化装置における生物膜処理管は、二重管構造を有するものに限らず、汚水による濾材の浸漬と空気による濾材の曝露とを間欠的に繰り返す構造を有する生物膜処理管であれば、固液分離管を接続することにより、目詰まりを防ぐ効果が大きく発揮される。
Since the solid 7 in the sewage 6 is separated by the solid-liquid separation tube 3, it does not flow out to the biofilm treatment tube 2, and only the supernatant water 9 is supplied to the biofilm treatment tube 2. Therefore, the solid matter 7 adheres to the biofilm of the biofilm treatment tube 2, or the biofilm treatment tube 2 includes an outer tube 10 and a water-permeable inner tube 11 as shown in FIG. In the case of the double tube structure, the solid matter 7 is prevented from clogging the microbial carrier 12 filled in the opening of the inner tube 11 and the gap between the inner tube 11 and the outer tube 10.
In addition, in FIG. 1, although the biofilm processing tube which has a double tube structure is described as the biofilm processing tube 2, the biofilm processing tube in the in-pipe purification apparatus of this invention has a double tube structure. If it is a biofilm treatment tube that has a structure that intermittently repeats immersion of filter media with sewage and exposure of filter media with air, it is effective to prevent clogging by connecting a solid-liquid separation tube. Demonstrated greatly.

固液分離管3には、固形物排出口13が設けられており、固液分離管3で分離された固形物7は、定期的にバキュームカー等で固形物排出口13から引き抜き廃棄される。 The solid-liquid separation tube 3 is provided with a solid material discharge port 13, and the solid material 7 separated by the solid-liquid separation tube 3 is periodically pulled out from the solid material discharge port 13 with a vacuum car or the like and discarded. .

本発明によれば、汚水中の固形物による目詰まりを防止し、安定的に汚水を処理できる管路内浄化装置を提供することができる。 ADVANTAGE OF THE INVENTION According to this invention, the clogging by the solid substance in wastewater can be prevented, and the in-pipe purification apparatus which can process a wastewater stably can be provided.

1 管路内浄化装置
2 生物膜処理管
3 固液分離管
4 汚水流入管
5 汚水流出管
6 汚水
7 固形物
8 越流堰
9 上澄水
10 外管
11 内管
12 微生物担体
13 固形物排出口
DESCRIPTION OF SYMBOLS 1 In-pipe purification apparatus 2 Biofilm processing pipe 3 Solid-liquid separation pipe 4 Sewage inflow pipe 5 Sewage outflow pipe 6 Sewage 7 Solid matter 8 Overflow weir 9 Supernatant water 10 Outer pipe 11 Inner pipe 12 Microorganism carrier 13 Solid matter outlet

Claims (5)

汚水を生物膜で処理する生物膜処理管と、該生物膜処理管へ汚水を供給する前に汚水を固液分離する固液分離管とを備え、
前記生物膜処理管は、汚水による濾材の浸漬と空気による濾材の曝露とを間欠的に繰り返す構造を有するとともに、前記固液分離管内の汚水の水位が上がり溢流することで上澄水が前記生物膜処理管に供給され
ことを特徴とする管路内浄化装置。
A biofilm treatment tube for treating sewage with a biofilm, and a solid-liquid separation tube for solid-liquid separation of sewage before supplying the sewage to the biofilm treatment tube ,
The biofilm treatment tube has a structure that intermittently repeats the immersion of the filter medium with sewage and the exposure of the filter medium with air, and the sewage water level in the solid-liquid separation pipe rises and overflows, so that the supernatant water becomes the organism. duct cleaning apparatus according to claim Rukoto supplied to the membrane process tube.
生物膜処理管は、生物膜の表面積が管路内面の表面積に対して10倍以上であることを特徴とする請求項1記載の管路内浄化装置。 The in-pipe purification apparatus according to claim 1, wherein the biofilm treatment tube has a biofilm surface area of 10 times or more of the surface area of the inner surface of the pipe line. 固液分離管は、越流堰を有することを特徴とする請求項1又は2記載の管路内浄化装置。The in-pipe purification apparatus according to claim 1 or 2, wherein the solid-liquid separation pipe has an overflow weir. 生物膜処理管は、外管と、透水性を有する内管とからなる二重管の外管と内管との間隙に微生物を坦持した担体が充填されている構造を有することを特徴とする請求項1、2又は3記載の管路内浄化装置。 The biofilm treatment tube has a structure in which a carrier carrying microorganisms is filled in a gap between an outer tube and an inner tube of a double tube composed of an outer tube and a water-permeable inner tube. The in-pipe purification apparatus according to claim 1, 2, or 3. 生物膜処理管及び固液分離管は、管路径方向の断面形状が円形であることを特徴とする請求項1、2、3又は4記載の管路内浄化装置。 The in-pipe purification apparatus according to claim 1, 2, 3, or 4, wherein the biofilm treatment pipe and the solid-liquid separation pipe have a circular cross-sectional shape in the pipe radial direction.
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