JP2008000705A - Sewage treatment apparatus of satellite treatment plant - Google Patents

Sewage treatment apparatus of satellite treatment plant Download PDF

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JP2008000705A
JP2008000705A JP2006173931A JP2006173931A JP2008000705A JP 2008000705 A JP2008000705 A JP 2008000705A JP 2006173931 A JP2006173931 A JP 2006173931A JP 2006173931 A JP2006173931 A JP 2006173931A JP 2008000705 A JP2008000705 A JP 2008000705A
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water
sewage
satellite
tank
treatment plant
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JP4844825B2 (en
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Yasuki Sekine
康記 関根
Kazuhiko Noto
一彦 能登
Kiyokazu Takemura
清和 武村
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Hitachi Plant Technologies 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
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Activated Sludge Processes (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
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Abstract

<P>PROBLEM TO BE SOLVED: To save a space of a sewage treatment apparatus in a satellite treatment plant. <P>SOLUTION: The sewage treatment apparatus 10 of the satellite treatment plant comprises a water-intake means 12 for taking water to be treated of the surface layer of sludge matter-containing sewage flowing through a sewer main line 18, a high-rate filter means 14 for performing solid-liquid separation with a filter medium layer 24 formed in a treatment tank 20, into which the water to be treated taken by the water-intake means 12 flows upward, by filling with a filter medium having a lower specific gravity than that of the water to be treated, and a membrane separation activated sludge means 16 for introducing the outflow water of the high-rate filter means 14 into an anaerobic tank 30 to anaerobically treat it, then introducing the outflow water from the anaerobic tank 30 into an aerobic tank 32 to aerobically treat it, and at the same time performing solid-liquid separation by a membrane separation part 36 installed in the aerobic tank 32. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、特に下水道幹線の上流側の下水道幹線から汚水の一部を採取し、汚水処理を行い下水道の上流側の市街地へ下水道の再利用水を供給するサテライト処理場の汚水処理装置に関する。   The present invention particularly relates to a sewage treatment apparatus for a satellite treatment plant that collects part of sewage from a sewage main line upstream of a sewage main line, performs sewage treatment, and supplies reused water of the sewage to an urban area upstream of the sewer.

図6はサテライト処理場の説明図である。図示のように下水道は、上流側から下流側に汚水を送水する下水道幹線1と、下水道幹線1の上流側に分岐して接続する複数の分岐管2と、下水道幹線1の下流側の末端に終末処理場3とを備えている。下水道は上流側の複数の分岐管2から流れてくる汚水を下水道幹線1で集水し、下流側の末端の終末処理場3において汚水を処理し下水道の再利用水を生成している。再利用水は、主に工業用処理水、雑用水、ビオトープ、河川水の確保、防火用水、緊急時生活用水などに利用されている。このような再利用水は下流側の処理場から上流側の市街地へ送水することは困難であり、終末処理場の近隣で多く利用されている。近年、下水道幹線の上流側の市街地に衛星的にサテライト処理場4を設けて、下水道の汚水処理を行い、処理場の近隣の市街地でも再利用水を利用できるようにしている。これにより、従来終末処理場の近隣で多く利用されていた再利用水を、下水道の上流側となる市街地でも有効的に活用することができる。   FIG. 6 is an explanatory diagram of a satellite treatment plant. As shown in the figure, the sewer is connected to a sewer main line 1 for sending sewage from the upstream side to the downstream side, a plurality of branch pipes 2 branched and connected to the upstream side of the sewer main line 1, and a downstream end of the sewer main line 1. And a final treatment plant 3. The sewer collects sewage flowing from a plurality of branch pipes 2 on the upstream side by a sewage main line 1 and processes the sewage at a terminal treatment plant 3 at the downstream end to generate reused water for the sewage. Recycled water is mainly used for industrial treated water, miscellaneous water, biotope, river water, fire prevention water, emergency life water, etc. Such recycled water is difficult to send from the downstream treatment plant to the upstream urban area, and is often used in the vicinity of the final treatment plant. In recent years, a satellite treatment plant 4 is provided in a satellite manner in an urban area upstream of a sewer main line to perform sewage treatment of the sewer so that reused water can be used also in an urban area near the treatment plant. This makes it possible to effectively use the reused water that has been widely used in the vicinity of the sewage treatment plant in the urban area upstream of the sewer.

ここで一般的な終末汚水処理場の処理工程について説明する。終末汚水処理場は、沈砂池および最初沈殿池による重力沈降を利用した固液分離設備である。図7に示すように下水道幹線から処理場まで流れてきた汚水は、まず沈砂池5に導入される。沈砂池5では流速を遅くして汚水中に含まれる大きな塵や砂を沈降させて汚水と分離させている。分離した汚水はポンプにより隣接する最初沈殿池6に導入される。最初沈殿池6では、前記沈砂池5よりもさらに遅い速度で沈砂池5で沈まなかった小さな塵を沈降させて汚水と分離させている。そして生物反応タンク7により汚水の活性汚泥反応が行われた後、最終沈殿池8で重力沈降を利用した固液分離を行う。その後、消毒設備9で減菌した後に河川や海域に放流される。(従来の膜分離活性汚泥装置は例えば特許文献1、2に開示されている。)
特許3257944号公報 特許3257946号公報
Here, the treatment process of a general terminal sewage treatment plant will be described. The terminal sewage treatment plant is a solid-liquid separation facility using gravity sedimentation by the sand basin and the first sedimentation basin. As shown in FIG. 7, the sewage flowing from the sewer main line to the treatment plant is first introduced into the sand basin 5. In the sand settling basin 5, the flow rate is slowed down so that large dust or sand contained in the sewage is settled and separated from the sewage. The separated sewage is introduced into the adjacent first settling basin 6 by a pump. In the first settling basin 6, small dust that has not settled in the settling basin 5 is settled at a slower speed than the settling basin 5 and separated from the sewage. Then, after the activated sludge reaction of sewage is performed in the biological reaction tank 7, solid-liquid separation using gravity sedimentation is performed in the final sedimentation tank 8. Then, after sterilization by the disinfection facility 9, it is discharged into rivers and sea areas. (A conventional membrane separation activated sludge apparatus is disclosed in, for example, Patent Documents 1 and 2.)
Japanese Patent No. 3257944 Japanese Patent No. 3257946

前記サテライト処理場は、広大な設置スペースを確保することが困難な市街地に配置するため省設置面積型であることが望ましく、活性汚泥濃度を高濃度に保つことで生物反応時間を短縮でき、かつ、生物反応槽中に膜分離装置を設置して固液分離を行うことで最終沈殿池ならびに消毒施設を省略できる膜分離活性汚泥法は、サテライト処理場に適しているといえる。   The satellite treatment plant is preferably a space-saving installation type because it is placed in an urban area where it is difficult to secure a large installation space, and the biological reaction time can be shortened by maintaining the activated sludge concentration at a high concentration, and The membrane separation activated sludge method, which can omit the final sedimentation basin and disinfection facility by installing a membrane separation device in the biological reaction tank and performing solid-liquid separation, can be said to be suitable for a satellite treatment plant.

一方、活性汚泥は、供給する原水性状により汚泥粘度が異なる傾向を示すことがわかっており、最初沈殿池の流入水と流出水を供給した場合を比較すると、バッキ槽内の活性汚泥浮遊物質の濃度:MLSS(Mixed Liquor Suspended Solid)が12g/lを超えた場合において、最初沈殿池の流入水を供給した場合に、粘度が高くなることがわかっている。粘度の上昇は微生物の代謝産物に由来する糖タンパク量が増加することが原因であるといわれているが、その増加機構は明らかになっていない。しかしながら、粘度が上昇すると活性汚泥のろ過性は低下し、薬品を用いた化学洗浄の頻度が多くなるため、維持管理性を考慮すると膜分離活性汚泥法への供給水は最初沈殿池の流出水と同等若しくは類似した水質であることが望ましい。   On the other hand, it is known that activated sludge tends to have different sludge viscosities depending on the raw water supply. Compared with the case where the inflow water and the outflow water of the first settling basin are supplied, the activated sludge suspended matter in the tank Concentration: When MLSS (Mixed Liquid Suspended Solid) exceeds 12 g / l, it is known that the viscosity increases when the inflow water of the first settling basin is supplied. The increase in viscosity is said to be caused by an increase in the amount of glycoprotein derived from microbial metabolites, but the mechanism of the increase is not clear. However, when the viscosity increases, the filterability of activated sludge decreases and the frequency of chemical cleaning with chemicals increases. Therefore, considering maintenance, the feed water to the membrane-separated activated sludge method is the effluent from the first sedimentation basin. It is desirable that the water quality is equivalent or similar to

ところで最初沈殿池は重力沈降を利用した固液分離設備であるため、例えば合流式下水道における固液分離速度は最大で50m/日までと制限され、広大な敷地面積が必要となる。敷地面積を縮小する手法としては、最初沈殿池の流入水中に有機系高分子凝集剤や無機系凝集剤を添加して粒子同士を結合させて沈殿速度の早い粒子を形成し、固液分離速度を速くする手法も考えられるが、薬品使用による維持管理コストの増加を考慮する必要が生じる。   By the way, since the first sedimentation basin is a solid-liquid separation facility using gravity sedimentation, for example, the solid-liquid separation speed in the combined sewer is limited to 50 m / day at the maximum, and a large site area is required. As a method to reduce the site area, first add organic polymer flocculant or inorganic flocculant into the inflow water of the sedimentation basin to combine the particles to form particles with high precipitation speed, solid-liquid separation speed Although a method for speeding up the process can be considered, it is necessary to consider an increase in maintenance cost due to the use of chemicals.

そこで本発明は従来技術の問題点を解決するため、サテライト処理場の汚水処理装置の省スペース化を図ることを目的としている。   SUMMARY OF THE INVENTION The present invention has been made to solve the problems of the prior art, and is intended to save space in a sewage treatment apparatus at a satellite treatment plant.

本発明のサテライト処理場の汚水処理装置は、下水道幹線の上流側に分岐したサテライト処理場を設け、前記下水道幹線の汚水の表層の一部を取水した被処理水の膜分離による汚水処理手段を備え、前記汚水処理手段の処理水を近隣の市街地へ供給することを特徴としている。   A sewage treatment apparatus for a satellite treatment plant according to the present invention is provided with a satellite treatment plant branched on the upstream side of a sewer main line, and a sewage treatment means by membrane separation of treated water that has taken a part of the surface layer of the sewage main line sewage. And the treated water of the sewage treatment means is supplied to a nearby urban area.

この場合において、前記汚水処理手段は、前記被処理水を処理槽内に形成したろ材層に加圧して流入させて固液分離を行う高速ろ過手段と、前記高速ろ過手段の排出口に直結し、前記高速ろ過手段からの流出水を嫌気槽に導入して嫌気処理し、前記嫌気槽からの流出水を好気槽に導入して好気処理するとともに、前記好気槽の内部に設けられた膜分離部で固液分離を行う膜分離活性汚泥手段と、を組み合わせたことを特徴としている。   In this case, the sewage treatment means is directly connected to a high-speed filtration means for performing solid-liquid separation by pressurizing and flowing the treated water into a filter medium layer formed in a treatment tank, and a discharge port of the high-speed filtration means. The effluent water from the high-speed filtration means is introduced into an anaerobic tank for anaerobic treatment, and the effluent water from the anaerobic tank is introduced into an aerobic tank for aerobic treatment, and is provided inside the aerobic tank. And a membrane separation activated sludge means for performing solid-liquid separation in the membrane separation unit.

この場合において、前記高速ろ過手段の被処理水の導入側には、前記導入側と前記下水道幹線との間の配管にフロートを備えた吸込み口を取り付け、前記下水道幹線を流れる汚水の表層の被処理水を取水する取水手段を備えているとよい。前記膜分離活性汚泥手段は、処理水の排出側に逆浸透膜またはナノろ過膜を取り付けているとよい。また前記膜分離活性汚泥手段は、処理槽内に活性炭を添加してあるとよい。   In this case, a suction port provided with a float is attached to a pipe between the introduction side and the sewer main line on the introduction side of the water to be treated of the high-speed filtration means, so that the surface layer of the sewage flowing through the sewer main line is covered. It is good to have a water intake means for taking treated water. The membrane separation activated sludge means may be provided with a reverse osmosis membrane or a nanofiltration membrane on the treated water discharge side. Moreover, the said membrane separation activated sludge means is good to have added activated carbon in the processing tank.

上記のごとくなっている本発明は、下水道幹線の上流側にサテライト処理場を設け、下水道幹線の汚水の表層の一部を取水した被処理水を高速ろ過手段と膜分離活性汚泥手段を直結し組み合わせて汚水処理を行っている。このため従来利用されている最初沈殿池の代替として高速ろ過設備を採用することで、サテライト処理場の敷地面積を大幅に削減することが可能となる。よって市街地の設置スペースの小さな場所であってもサテライト処理場を設置することができる。また高速ろ過手段は設置面積の省スペース化を実現できるとともに、高速ろ過手段の流出水を後段の膜分離活性汚泥手段に供給することで汚泥粘度の上昇を抑制できるため、安定した膜分離活性汚泥手段の稼動が可能となり、汚水処理の処理コストを低減することができる。   In the present invention as described above, a satellite treatment plant is provided on the upstream side of the sewer main line, and the treated water that has taken a part of the surface layer of the sewage main line is directly connected to the high-speed filtration means and the membrane separation activated sludge means. Sewage treatment is performed in combination. For this reason, it is possible to significantly reduce the site area of the satellite treatment plant by adopting high-speed filtration equipment as an alternative to the first settling basin that has been conventionally used. Therefore, a satellite treatment plant can be installed even in a small installation space in an urban area. In addition, the high-speed filtration means can reduce the installation area and supply the effluent water from the high-speed filtration means to the membrane separation activated sludge means in the subsequent stage to suppress the increase in sludge viscosity. The operation of the means becomes possible, and the treatment cost of sewage treatment can be reduced.

本発明の被処理水の取水手段は、汚水の表層の一部を取水するようにしている。このため汚水に含まれる汚泥物質の取水を軽減し、汚水処理装置の浄化処理の負担を軽減するこができる。   The means for taking water to be treated of the present invention takes a part of the surface layer of sewage. For this reason, the intake of the sludge substance contained in sewage can be reduced, and the burden of the purification process of a sewage treatment apparatus can be reduced.

本発明の膜分離活性汚泥手段の後段には、逆浸透膜またはナノろ過膜を取り付けている。逆浸透膜は水に含まれる無機分子を除去することができ、飲料水に近い清浄度が得られる。またナノろ過膜は、被処理水の色度成分を除去し透明の処理水が得られる。よって逆浸透膜またはナノろ過膜を任意に選択することにより用途に応じた再利用水を得ることができる。   A reverse osmosis membrane or a nanofiltration membrane is attached to the subsequent stage of the membrane separation activated sludge means of the present invention. The reverse osmosis membrane can remove inorganic molecules contained in water, and a cleanness close to that of drinking water can be obtained. In addition, the nanofiltration membrane removes the chromaticity component of the water to be treated to obtain transparent treated water. Therefore, by selecting a reverse osmosis membrane or a nanofiltration membrane arbitrarily, reused water can be obtained according to the application.

本発明の膜分離活性汚泥手段には活性炭を添加している。このため活性汚泥反応とともに、被処理水の脱臭、水質浄化、吸着等の効果が得られる。また膜分離部により活性炭と処理水を容易に分離することができる。   Activated carbon is added to the membrane separation activated sludge means of the present invention. For this reason, effects such as deodorization of water to be treated, water purification, adsorption and the like are obtained along with the activated sludge reaction. Moreover, activated carbon and treated water can be easily separated by the membrane separation unit.

本発明のサテライト処理場の汚水処理装置の実施形態を添付の図面を参照しながら以下詳細に説明する。図1は実施形態に係るサテライト処理場の汚水処理装置の構成概略を示す図である。図2は実施形態に係るサテライト処理場の汚水処理装置の説明図である。   An embodiment of a sewage treatment apparatus for a satellite treatment plant according to the present invention will be described in detail below with reference to the accompanying drawings. Drawing 1 is a figure showing the composition outline of the sewage treatment equipment of the satellite treatment plant concerning an embodiment. FIG. 2 is an explanatory diagram of the sewage treatment apparatus of the satellite treatment plant according to the embodiment.

サテライト処理場の汚水処理装置10を設置するサテライト処理場は、下水道幹線18の上流側であって複数の市街地に設置している。またサテライト処理場は、下水道幹線18と市街地との間に形成し下水道幹線18の汚水の一部を取水するようにしている。図示のようにサテライト処理場に設置する汚水処理装置10は、被処理水の取水手段12と、汚水処理手段となる高速ろ過手段14と、膜分離活性汚泥手段16とを基本構成としている。   The satellite treatment plant where the sewage treatment apparatus 10 of the satellite treatment plant is installed is installed in a plurality of urban areas on the upstream side of the sewer main line 18. In addition, the satellite treatment plant is formed between the sewer main line 18 and the city area and takes a part of the sewage from the sewer main line 18. As shown in the figure, a sewage treatment apparatus 10 installed in a satellite treatment plant has a basic configuration of water intake means 12 for water to be treated, high-speed filtration means 14 serving as sewage treatment means, and membrane separation activated sludge means 16.

汚水処理装置10は、図2に示すように下水道幹線18から取水した汚水を導入している。取水手段12は、下水道幹線18と高速ろ過手段14の導入口間を接続する配管13の途中にポンプ15を取り付け、配管13の端部にホース13aを備えた構成である。また下水道幹線18側のホース13aの吸込み口17はフロート19などの浮体を介して下水道幹線18を流れる汚染物質を含む汚水上を浮上させ表層付近に取り付けている。そして配管端部が汚水上を浮遊しながら配管端部の吸込み口17からポンプ15の吸引によって表層水を取水している。   The sewage treatment apparatus 10 introduces sewage taken from the sewer main line 18 as shown in FIG. The water intake means 12 has a configuration in which a pump 15 is attached in the middle of a pipe 13 connecting between the sewer main line 18 and the inlet of the high-speed filtration means 14, and a hose 13 a is provided at the end of the pipe 13. The suction port 17 of the hose 13a on the sewer main line 18 side is floated on the sewage containing pollutants flowing through the sewer main line 18 via a floating body such as a float 19 and attached near the surface layer. And the surface water is taken in by suction of the pump 15 from the suction port 17 at the pipe end while the pipe end floats on the sewage.

高速ろ過手段14は、処理槽20内の下方に汚水の導入口22を備えている。また処理槽20内の上方には水平方向にろ材層24を形成し、上端部に処理水の排出口26を取り付けている。ろ材層24は、被処理水より比重の小さなろ材、例えば比重が1以下であり吸水性のないポリプロピレンを用いたろ材をろ材よりも小さな目開きを有するスクリーンで保護することにより、外部への流出を防止している。処理槽20の下方には引抜管21を取り付け、処理槽20内の下方に堆積した汚泥または洗浄排水を外部に排出するようにしている。なおこの洗浄排水は下水道幹線18に取り付けた取水手段12よりも下流側に接続させて、下水道に戻すように構成することもできる。   The high speed filtration means 14 includes a sewage introduction port 22 below the processing tank 20. Further, a filter medium layer 24 is formed in the horizontal direction above the inside of the treatment tank 20, and a treated water discharge port 26 is attached to the upper end portion. The filter medium layer 24 flows out to the outside by protecting a filter medium having a specific gravity smaller than that of the water to be treated, for example, a filter medium having a specific gravity of 1 or less and having no water absorption with a screen having a smaller opening than the filter medium. Is preventing. A drawing tube 21 is attached below the treatment tank 20 so that sludge or washing wastewater deposited below the treatment tank 20 is discharged to the outside. The washing waste water may be connected downstream of the water intake means 12 attached to the sewer main line 18 and returned to the sewer.

膜分離活性汚泥手段16は、嫌気槽30と、好気槽32を備えている。嫌気槽30および好気槽32は複数の仕切板33を介して隣接配置してある。また嫌気槽30および好気槽32は循環経路34を設けて活性汚泥を循環させている。嫌気槽30の導入口は、高速ろ過手段14の排出口26と配管23を介して直結させている。嫌気槽30の槽内には高速ろ過手段14からの被処理水を導入させている。嫌気槽30内では被処理水を活性汚泥処理している。   The membrane separation activated sludge means 16 includes an anaerobic tank 30 and an aerobic tank 32. The anaerobic tank 30 and the aerobic tank 32 are arranged adjacent to each other via a plurality of partition plates 33. The anaerobic tank 30 and the aerobic tank 32 are provided with a circulation path 34 to circulate activated sludge. The introduction port of the anaerobic tank 30 is directly connected to the discharge port 26 of the high-speed filtration means 14 via the pipe 23. The water to be treated from the high speed filtration means 14 is introduced into the anaerobic tank 30. In the anaerobic tank 30, the water to be treated is treated with activated sludge.

また好気槽32は嫌気槽30からの活性汚泥処理水を導入して好気処理するとともに、槽内に設けられた膜分離部36で固液分離を行っている。膜分離部36は、ケーシング内に複数のろ過膜を並列配置し、ケーシング上部に接続する配管37から吸引ポンプや、水頭差を利用した重力ろ過により膜透過水(処理水)を外部に排出するようにしている。また膜分離部36の下方の好気槽32には散気手段38を取り付けてある。散気手段38は好気槽32の底面から所定の位置に離間して配置してある。   The aerobic tank 32 introduces activated sludge treated water from the anaerobic tank 30 for aerobic treatment, and performs solid-liquid separation by a membrane separation unit 36 provided in the tank. The membrane separation unit 36 arranges a plurality of filtration membranes in the casing in parallel, and discharges the membrane permeated water (treated water) from the piping 37 connected to the upper portion of the casing to the outside by a suction pump or gravity filtration using a water head difference. I am doing so. An aeration means 38 is attached to the aerobic tank 32 below the membrane separation unit 36. The air diffuser 38 is spaced from the bottom surface of the aerobic tank 32 at a predetermined position.

好気槽32の下方には、余剰汚泥の引抜管40を形成してあり、好気槽32の余剰汚泥を外部に排出するようにしている。また前記同様にこの余剰汚泥は下水道幹線18に取り付けた取水手段12よりも下流側に接続させて、下水道に戻すように構成することもできる。   A surplus sludge extraction pipe 40 is formed below the aerobic tank 32 so that the excess sludge in the aerobic tank 32 is discharged to the outside. Similarly to the above, this excess sludge can be connected to the downstream side of the water intake means 12 attached to the sewer main line 18 and returned to the sewer.

上記構成によるサテライト処理場の汚水処理装置10は以下のように作用する。下水道幹線18の上流側であって、下水道再処理水の需要がある市街地には複数のサテライト処理場を設けている。サテライト処理場は、被処理水の取水手段12が下水道幹線18に接続している。被処理水の取水手段12は、配管13の吸込み口17をフロート19を介して下水道幹線18を流れる汚水上に浮かべてあり、配管途中に設けたポンプの吸引により汚染物質を含む汚水の表層の被処理水のみを取水する。下水道幹線18は、降雨量などにより排水量が異なる。そこで下水道幹線側の配管端部にフロート19を設けることにより、下水道の底面に堆積している汚泥物質を吸引することなく、汚水の表層部分の被処理水を取水することができる。これにより、下水道幹線の汚水中に含まれる汚泥物質の取水を軽減し汚水処理装置10の浄化処理の負担を軽減することができる。   The sewage treatment apparatus 10 in the satellite treatment plant having the above-described configuration operates as follows. A plurality of satellite treatment plants are provided on the upstream side of the sewer main line 18 and in an urban area where there is a demand for sewer reprocessing water. In the satellite treatment plant, the water intake means 12 for the treated water is connected to the sewer main line 18. The water intake means 12 of the treated water floats the suction port 17 of the pipe 13 on the sewage flowing through the sewer main line 18 via the float 19, and the surface layer of the sewage containing pollutants by suction of a pump provided in the middle of the pipe. Take only treated water. The amount of drainage of the sewer main line 18 varies depending on the amount of rainfall. Therefore, by providing the float 19 at the pipe end on the sewer main line side, the water to be treated in the surface layer portion of the sewage can be taken without sucking the sludge accumulated on the bottom surface of the sewer. Thereby, the intake of the sludge substance contained in the sewage of a sewer main line can be reduced, and the burden of the purification process of the sewage treatment apparatus 10 can be reduced.

取水手段12により下水道幹線18の汚水の一部を取水した被処理水は、配管13を介して高速ろ過手段14の導入口22から処理槽20内部に導入される。処理槽20に導入された被処理水は、処理槽20の上方に形成した排出口26に向かって流れる。被処理水は、ろ材層24のろ材間を通過するときに被処理水中の大きな汚泥物質が取り除かれる。高速ろ過手段14を通過した処理水は、従来の最初沈殿池を通過した処理水と同程度の清浄度を保持している。また高速ろ過手段14は従来の沈砂池および最初沈殿池を備えた処理場に比べ設置スペースを大幅に縮小することができる。   The water to be treated which has taken a part of the sewage from the sewer main line 18 by the water intake means 12 is introduced into the treatment tank 20 from the introduction port 22 of the high speed filtration means 14 through the pipe 13. The water to be treated introduced into the treatment tank 20 flows toward the discharge port 26 formed above the treatment tank 20. When the water to be treated passes between the filter media of the filter media layer 24, a large sludge substance in the water to be treated is removed. The treated water that has passed through the high-speed filtration means 14 maintains the same level of cleanness as the treated water that has passed through the conventional first sedimentation basin. Moreover, the high-speed filtration means 14 can reduce installation space significantly compared with the treatment plant provided with the conventional sedimentation basin and the first sedimentation basin.

本発明の汚水処理装置10は、高速ろ過手段14と膜分離活性汚泥手段16とを直結し組み合わせた構成であり、高速ろ過手段14を通過した被処理水は、排出口26から直結する膜分離活性汚泥手段16の導入口へ導入される。膜分離活性汚泥手段16の嫌気槽30に導入された被処理水は、所定の濃度に調整された活性汚泥によって生物反応が行われる。そして隣接する好気槽32に活性汚泥処理水が導入され、処理槽内部に設けた膜分離部36から吸引される。膜分離膜36は複数のろ過膜を並列配置してあり、ろ過膜によって処理水と活性汚泥とを分離し、ろ過膜を通過した処理水は再利用水として外部に放出される。なお高速ろ過手段と膜分離活性汚泥手段は一体構造とし、高速ろ過手段の処理槽と、膜分離活性汚泥手段の嫌気槽と、好気槽とを並べて配置し、省スペース化を図るようにしてもよい。   The sewage treatment apparatus 10 of the present invention has a configuration in which the high-speed filtration means 14 and the membrane separation activated sludge means 16 are directly connected and combined, and the treated water that has passed through the high-speed filtration means 14 is membrane-separated directly from the discharge port 26. It is introduced into the inlet of the activated sludge means 16. The treated water introduced into the anaerobic tank 30 of the membrane separation activated sludge means 16 undergoes a biological reaction with the activated sludge adjusted to a predetermined concentration. Then, the activated sludge treated water is introduced into the adjacent aerobic tank 32 and sucked from the membrane separation unit 36 provided inside the treatment tank. The membrane separation membrane 36 has a plurality of filtration membranes arranged in parallel, and the treated water and activated sludge are separated by the filtration membrane, and the treated water that has passed through the filtration membrane is discharged to the outside as reused water. The high-speed filtration means and the membrane separation activated sludge means are integrated, and the processing tank of the high-speed filtration means, the anaerobic tank of the membrane separation activated sludge means, and the aerobic tank are arranged side by side to save space. Also good.

図3は実施形態に係る汚水処理装置の第1変形例の説明図である。図示のように汚水処理装置の第1変形例は、膜分離活性汚泥手段16による処理水の流出経路に逆浸透膜(RO膜)またはナノろ過膜(NF膜)を取り付けている。逆浸透膜(RO膜)は、被処理水を通過させることにより、水に含まれる無機分子を除去することができ、飲料水に近い清浄度が得られる。またナノろ過膜(NF膜)は、処理水を通過させることにより被処理水中に含まれる色度成分を除去し透明の処理水とすることができる。このように膜分離活性汚泥手段16により処理された処理水は、逆浸透膜またはナノろ過膜を任意に選択することにより、用途に応じた再利用水を得ることができる。   FIG. 3 is an explanatory diagram of a first modification of the sewage treatment apparatus according to the embodiment. As shown in the figure, in the first modification of the sewage treatment apparatus, a reverse osmosis membrane (RO membrane) or a nanofiltration membrane (NF membrane) is attached to the treated water outflow path by the membrane separation activated sludge means 16. The reverse osmosis membrane (RO membrane) can remove inorganic molecules contained in the water by allowing the water to be treated to pass through, and a cleanliness level close to that of drinking water can be obtained. Moreover, the nanofiltration membrane (NF membrane) can remove the chromaticity component contained in to-be-processed water by letting treated water pass, and can set it as transparent treated water. As described above, the treated water treated by the membrane separation activated sludge means 16 can select reused osmosis membrane or nanofiltration membrane to obtain reused water according to the intended use.

図4は実施形態に係る汚水処理装置の第2変形例の説明図である。図示のように汚水処理装置の第2変形例は、膜分離活性汚泥手段16の嫌気槽30および好気槽32に活性炭42を添加している。活性炭42は多孔質であるとともに吸着性があり、脱臭、水質浄化、吸着等の効果が知られている。これにより、膜分離活性汚泥手段16による活性汚泥処理反応とともに被処理水の脱色を行うことができる。なお添加された活性炭42は、膜分離部36によって処理水と容易に分離することができる。   FIG. 4 is an explanatory diagram of a second modification of the sewage treatment apparatus according to the embodiment. As shown in the figure, in the second modification of the sewage treatment apparatus, activated carbon 42 is added to the anaerobic tank 30 and the aerobic tank 32 of the membrane separation activated sludge means 16. The activated carbon 42 is porous and adsorbable, and effects such as deodorization, water purification and adsorption are known. As a result, the water to be treated can be decolored together with the activated sludge treatment reaction by the membrane separation activated sludge means 16. The added activated carbon 42 can be easily separated from the treated water by the membrane separation unit 36.

図5は実施形態に係る取水手段の変形例を示す図である。同図(1)に示すように配管13の端部を下水道幹線18の汚水の流れに対し垂直方向であって、底面から所定の間隔を開けて取り付け、配管13の側面に開口部13bを複数並べて形成してある。そして配管13の直径よりも大径となる外筒44を配管13の端部に取り付ける。外筒44は比重を1よりも小さい材質を用いているため、汚水上に浮上し、外筒44の下端部から露出した開口部13bから汚水を取水できる。また同図(2)に示すように配管13の端部には、可動配管46を矢印aに示す方向に回動可能なジョイントを介して取り付けている。可動配管46は、比重を1よりも小さい材質を用いるか、あるいはフロート19を開口に取り付けることにより、汚水上に浮上しやすくなり、汚水の表層水を取水することができる。   FIG. 5 is a view showing a modification of the water intake means according to the embodiment. As shown in FIG. 1 (1), the end of the pipe 13 is attached in a direction perpendicular to the sewage flow of the sewer main line 18 at a predetermined interval from the bottom, and a plurality of openings 13b are provided on the side of the pipe 13. They are formed side by side. Then, an outer cylinder 44 having a diameter larger than that of the pipe 13 is attached to the end of the pipe 13. Since the outer cylinder 44 is made of a material having a specific gravity smaller than 1, the outer cylinder 44 floats on the sewage and can take sewage from the opening 13 b exposed from the lower end of the outer cylinder 44. As shown in FIG. 2B, the movable pipe 46 is attached to the end of the pipe 13 via a joint that can rotate in the direction indicated by the arrow a. The movable pipe 46 is made of a material having a specific gravity smaller than 1, or the float 19 is attached to the opening, so that the movable pipe 46 can easily float on the sewage and take up the surface water of the sewage.

以上説明したようにこのようなサテライト処理場の汚水処理装置によれば、サテライト処理場における膜分離活性汚泥設備の安定運転のために、最初沈殿池の代替として高速ろ過設備を採用し、高速ろ過手段と膜分離活性汚泥手段を組み合わせることにより、サテライト処理場の敷地面積を大幅に削減することができる。本発明によれば例えば高速ろ過手段の固液分離速度を400m/日とした場合、必要面積は従来の最初沈殿池を採用した処理場の場合の1/8以下となる。また高速ろ過手段の流出水を膜分離活性汚泥手段に供給することで汚泥粘度の上昇を抑制するため、安定した膜分離活性汚泥装置の稼動が可能となり、汚水の処理コストを低減することが可能となる。   As described above, according to the sewage treatment apparatus of such a satellite treatment plant, a high-speed filtration facility is adopted as an alternative to the first sedimentation basin for the stable operation of the membrane separation activated sludge facility in the satellite treatment plant, and the high-speed filtration is performed. By combining the means and membrane separation activated sludge means, the site area of the satellite treatment plant can be greatly reduced. According to the present invention, for example, when the solid-liquid separation speed of the high-speed filtration means is 400 m / day, the required area is 1/8 or less of that in the case of a treatment plant employing a conventional first sedimentation basin. In addition, by supplying the effluent from the high-speed filtration means to the membrane separation activated sludge means, it is possible to operate the membrane separation activated sludge apparatus stably because the increase in sludge viscosity is suppressed, and it is possible to reduce the treatment cost of the sewage. It becomes.

サテライト処理場の汚水処理装置の構成概略を示す図である。It is a figure which shows the structure outline of the sewage treatment apparatus of a satellite treatment plant. サテライト処理場の汚水処理装置の説明図である。It is explanatory drawing of the sewage treatment apparatus of a satellite treatment plant. 汚水処理装置の第1変形例の説明図である。It is explanatory drawing of the 1st modification of a sewage treatment apparatus. 汚水処理装置の第2変形例の説明図である。It is explanatory drawing of the 2nd modification of a sewage treatment apparatus. 実施形態に係る取水手段の変形例の説明図である。It is explanatory drawing of the modification of the water intake means which concerns on embodiment. サテライト処理場の説明図である。It is explanatory drawing of a satellite treatment plant. 従来の処理場の処理工程の説明図である。It is explanatory drawing of the treatment process of the conventional treatment plant.

符号の説明Explanation of symbols

1………下水道幹線、2………分岐管、3………終末処理場、4………サテライト処理場、5………沈砂池、6………最初沈殿池、7………生物反応タンク、8………最終沈殿池、9………消毒設備、10………汚水処理装置、12………取水手段、13………配管、14………高速ろ過手段、15………ポンプ、16………膜分離活性汚泥手段、17………吸込み口、18………下水道幹線、19………フロート、20………処理槽、21………引抜管、22………導入口、23………配管、24………ろ材層、26………排出口、30………嫌気槽、32………好気槽、33………仕切板、34………循環経路、36………膜分離部、37………配管、38………散気手段、40………引抜管、42………活性炭、44………外筒、46………可動配管。 1 ......... Sewer main line, 2 ......... Branch pipe, 3 ......... Sewage treatment plant, 4 ...... Satellite treatment plant, 5 ...... Sedimentation basin, 6 ......... First sedimentation basin, 7 ... Reaction tank, 8 ......... Final sedimentation basin, 9 ......... Disinfection equipment, 10 ......... Sewage treatment equipment, 12 ......... Water intake means, 13 ......... Piping, 14 ...... High-speed filtration means, 15 ... ... Pump, 16 ......... Membrane separation activated sludge means, 17 ......... Suction port, 18 ......... Sewer main line, 19 ......... Float, 20 ...... Treatment tank, 21 ...... Drawer, 22 ... ... Introduction port, 23 ...... Piping, 24 ......... Filter medium layer, 26 ......... Discharge port, 30 ...... Anaerobic tank, 32 ...... Aerobic tank, 33 ......... Partition plate, 34 ......... Circulation path, 36 ......... Membrane separation part, 37 ......... Piping, 38 ......... Aeration means, 40 ...... Drawing pipe, 42 ......... Activated carbon, 44 ...... Outer cylinder, 46 ...... moveable pipe.

Claims (5)

下水道幹線の上流側に分岐したサテライト処理場を設け、前記下水道幹線の汚水の表層の一部を取水した被処理水の膜分離による汚水処理手段を備え、前記汚水処理手段の処理水を近隣の市街地へ供給することを特徴とするサテライト処理場の汚水処理装置。   A satellite treatment plant branching upstream of the sewer main line is provided, and includes a sewage treatment means by membrane separation of treated water that has taken a part of the surface layer of the sewage main line, and the treated water of the sewage treatment means is disposed in the vicinity. A sewage treatment apparatus for a satellite treatment plant, characterized by being supplied to an urban area. 前記汚水処理手段は、
前記被処理水を処理槽内に形成したろ材層に加圧して流入させて固液分離を行う高速ろ過手段と、
前記高速ろ過手段の排出口に直結し、前記高速ろ過手段からの流出水を嫌気槽に導入して嫌気処理し、前記嫌気槽からの流出水を好気槽に導入して好気処理するとともに、前記好気槽の内部に設けられた膜分離部で固液分離を行う膜分離活性汚泥手段と、
を組み合わせたことを特徴とする請求項1記載のサテライト処理場の汚水処理装置。
The sewage treatment means includes
High-speed filtration means for performing solid-liquid separation by pressurizing and flowing the water to be treated into a filter medium layer formed in a treatment tank;
Directly connected to the discharge port of the high-speed filtration means, introduces effluent water from the high-speed filtration means into an anaerobic tank and anaerobically treats it, and introduces effluent water from the anaerobic tank into an aerobic tank for aerobic treatment. A membrane separation activated sludge means for performing solid-liquid separation in a membrane separation section provided in the aerobic tank;
The sewage treatment apparatus for a satellite treatment plant according to claim 1, wherein
前記高速ろ過手段の被処理水の導入側には、前記導入側と前記下水道幹線との間の配管にフロートを備えた吸込み口を取り付け、前記下水道幹線を流れる汚水の表層の被処理水を取水する取水手段を備えていることを特徴とする請求項2記載のサテライト処理場の汚水処理装置。   A suction port having a float is attached to a pipe between the introduction side and the sewer main line on the introduction side of the treated water of the high-speed filtration means, and the treated water of the surface layer of sewage flowing through the sewer main line is taken. The sewage treatment apparatus for a satellite treatment plant according to claim 2, further comprising water intake means for carrying out the process. 前記膜分離活性汚泥手段は、処理水の排出側に逆浸透膜またはナノろ過膜を取り付けていることを特徴とする請求項2または3に記載のサテライト処理場の汚水処理装置。   The sewage treatment apparatus for a satellite treatment plant according to claim 2 or 3, wherein the membrane separation activated sludge means has a reverse osmosis membrane or a nanofiltration membrane attached to the treated water discharge side. 前記膜分離活性汚泥手段は、処理槽内に活性炭を添加してあることを特徴とする請求項2乃至4のいずれか記載のサテライト処理場の汚泥処理装置。   The sludge treatment apparatus for a satellite treatment plant according to any one of claims 2 to 4, wherein the membrane separation activated sludge means has activated carbon added to a treatment tank.
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