WO2002081050A1 - Dispositif de traitement des eaux de pluie dans des eaux d'egout mixtes et procede de lavage a contre-courant associe - Google Patents
Dispositif de traitement des eaux de pluie dans des eaux d'egout mixtes et procede de lavage a contre-courant associe Download PDFInfo
- Publication number
- WO2002081050A1 WO2002081050A1 PCT/JP2002/003404 JP0203404W WO02081050A1 WO 2002081050 A1 WO2002081050 A1 WO 2002081050A1 JP 0203404 W JP0203404 W JP 0203404W WO 02081050 A1 WO02081050 A1 WO 02081050A1
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- WO
- WIPO (PCT)
- Prior art keywords
- rainwater
- tank
- treatment
- sewage
- speed filtration
- Prior art date
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/002—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with multiple filtering elements in parallel connection
- B01D24/005—Filters being divided into a plurality of cells or compartments
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/02—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed stationary during the filtration
- B01D24/20—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed stationary during the filtration the filtering material being provided in an open container
- B01D24/26—Upward filtration
- B01D24/263—Upward filtration the filtering material being supported by pervious surfaces
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- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S210/00—Liquid purification or separation
- Y10S210/918—Miscellaneous specific techniques
- Y10S210/919—Miscellaneous specific techniques using combined systems by merging parallel diverse waste systems
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S210/00—Liquid purification or separation
- Y10S210/918—Miscellaneous specific techniques
- Y10S210/92—Miscellaneous specific techniques using combined systems of sequential local and regional or municipal sewage systems
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S210/00—Liquid purification or separation
- Y10S210/918—Miscellaneous specific techniques
- Y10S210/921—Flow equalization or time controlled stages or cycles
Definitions
- the present invention relates to a rainwater treatment apparatus in a combined sewer system in which sewage and rainwater are combined as sewage, and a backwash method thereof. Furthermore, the present invention relates to a sewage treatment system using a sewage treatment apparatus for rainy weather (hereinafter referred to as a stormwater treatment apparatus).
- a stormwater treatment apparatus a sewage treatment apparatus for rainy weather
- the term rainwater is used to mean sewage, which is the confluence of rainwater and sewage during rainfall. I do.
- the design maximum water flow rate is the maximum maximum inflow flow rate when there is no rainwater.
- the present invention solves the conventional problems described above, and can remove most of the pollutants even when rainwater exceeding Q or even a large amount of rainwater exceeding 3 Q flows. This was made to provide a rainwater treatment system for a combined sewer system that can be used. Further, the present invention provides a rainwater treatment apparatus which can be installed at a low cost by simply modifying an existing first sedimentation basin when installing the rainwater treatment apparatus, and a backwash method thereof. Another object of the present invention is to provide a rainwater treatment apparatus for a combined sewer system and a method for backwashing the same, which can achieve the above object with almost no maintenance. Further, the present invention relates to a sewage treatment system using the rainwater treatment device.
- a first aspect of the present invention is to provide a plurality of upward-flow type high-speed filtration tanks having a floating filter medium layer, and upper surfaces of the plurality of high-speed filtration tanks.
- a common treatment tank for collecting treated water from the high-speed filtration tank, a washing drainage tank for collecting washing wastewater from each high-speed filtration tank, and a rainwater inflow channel for distributing rainwater flowing into the upper part of the plurality of high-speed filtration tanks.
- a rainwater treatment device for a combined sewer system comprising: a rainwater inflow section for flowing rainwater distributed from a water inflow channel below the floating filter medium layer of each high-speed filtration tank. .
- the rainwater treatment apparatus according to the present invention can form the rainwater treatment apparatus by partitioning the first sedimentation basin of the conventional combined sewage treatment plant.
- a second viewpoint of the present invention is a first sewage treatment section including a sedimentation basin that receives sewage, a first sedimentation basin provided downstream of the sedimentation basin, and a reaction tank provided downstream of the sedimentation basin.
- a sewage treatment system in a combined sewerage system comprising a second sewage treatment unit provided downstream of the sand basin, wherein the second sewage treatment unit is provided with a plurality of upward-flow high-speed type having a floating filter medium layer.
- a filtration tank a common treatment water tank provided on an upper surface of the plurality of high-speed filtration tanks for collecting processing tanks from the high-speed filtration tank; a washing drainage tank for collecting washing wastewater from each high-speed filtration tank; A rainwater inflow channel for distributing inflow rainwater at the top of the tank, and a rainwater inflow portion for allowing rainwater distributed from the water inflow channel to flow below the floating filter medium layer of each high-speed filtration tank; If the amount of sewage is less than the specified design water volume, the sewage treatment is performed in the first sewage treatment unit.
- the amount of sewage exceeding the specified design water volume For about sewage treatment system in the combined sewer system, characterized in can der Rukoto performing the sewage treatment in the second sewage treatment unit.
- the rainwater treatment apparatus of the present invention can accommodate an existing, for example, a first sedimentation basin with a tank height of 2.5 to 4 m by being modified.
- the thickness can be as thin as 0.5 to 1 m, less than 2 m, and a compact high-speed filtration equipment that does not require a lower screen and does not require equipment for adding a flocculant can be realized.
- the reason for this is that a plurality of high-speed filtration tanks were provided to reduce the amount of water, and the layer thickness of the common treatment tank was reduced.
- the rainwater treatment apparatus in the combined sewer system and the method for backwashing the sewage system according to the present invention are the above-described rainwater treatment apparatus in the combined sewer system, wherein the treated wastewater in the common treated water tank is removed from the high-speed filtration tank with increased pressure loss. It is characterized by performing backwash by flowing water downward.
- the first sedimentation basin of the combined sewage treatment plant is divided into A high-speed filtration tank is installed to distribute a large amount of rainwater that flows in during rainfall to each tank through a rainwater inflow channel, and high-speed filtration can be performed with the filled floating filter medium. Therefore, most of the pollutants can be removed even when rainwater exceeding Q or even large amounts of rainwater exceeding 3 Q flows. Also, since a part of the existing first sedimentation basin is divided and high-speed filtration tanks are installed, it is not necessary to construct new civil engineering equipment and secure installation space. As will be described in further detail below, the present invention can be operated with little maintenance.
- FIG. 1 is a plan view showing a rainwater treatment apparatus according to an embodiment of the present invention.
- FIG. 2 is a vertical sectional view of FIG.
- Figure 3 is a vertical sectional view showing the rainwater inflow channel.
- FIG. 4 is a plan view and a sectional view showing the flow of rainwater at the start of rainfall.
- FIG. 5 is a plan view and a sectional view showing the flow of rainwater during the continuation of rainfall.
- FIG. 6 is a plan view and a cross-sectional view showing the flow of rainwater during backwashing of one tank while rainfall continues.
- FIG. 7 shows a filter medium having four arms that can be used in the present invention.
- FIG. 8 shows a filter medium in which corrugated irregularities are formed on the outer peripheral surface of a plate-like body having a rectangular cross section which can be used in the present invention and which can be used in the present invention.
- FIG. 9 shows a filter medium having a Z-shaped cross section that can be used in the present invention.
- FIG. 10 shows a filter medium on a tube that can be used in the present invention.
- FIG. 11 shows a windmill-type filter medium in which the blade portion of FIG. 7 can be used in the present invention.
- FIG. 1 is a plan view showing a rainwater treatment apparatus of the present invention
- FIG. 2 is a cross-sectional view taken along the line II-II of FIG.
- the first sedimentation installed in the combined sewage treatment plant Of the ponds
- the necessary amount of the ponds is left as it is in the conventional first sedimentation basin 1 (in the figure, the two rows of the first sedimentation basin).
- two rows of high-speed filtration tank and washing drainage tank are used.
- the water area of the first sedimentation basin 1 is smaller than before, but due to advances in sewage treatment technology, the water area of the first sedimentation basin 1 has recently become smaller and smaller than before.
- the initial sedimentation basin 1 often has excess treatment capacity, so there is no effect on normal sewage treatment. Or, as a result, the first settling basin will only accept up to the maximum amount of sewage during clear weather hours, so there is no impact on normal sewage treatment.
- the left part of Fig. 1 is provided with a sedimentation basin 5 for supplying sewage, a rainwater tank 6 for distributing sewage from the sedimentation basin based on the set water amount and rainfall, and a sewage tank 7. .
- the rainwater tank 6 and the sewage tank 7 may be a common tank.
- the entire amount of incoming sewage is received in the sedimentation basin 5, and up to the design water volume of 3Q is led to the conventional first sedimentation basin 1 by the sewage pump 8.
- the water from which SS has been separated in the first settling tank 1 is sent to the subsequent reaction tank, where it is treated as usual. Since the amount of incoming sewage is less than Q in fine weather, it is the same as before that only this line is operated.
- the entire amount exceeding Q is guided to the high-speed filtration tank 3 side. Therefore, if necessary, the water pipe from the sewage pump 8 will be remodeled to lead to the high-speed filtration tank 3.
- the high-speed filtration tank 3 is a filtration tank in which a screen 10 is provided in the middle part and a floating filter medium 11 is filled below the screen.
- a total of eight tanks are arranged in two rows, but the number is arbitrary as long as the number of tanks is plural.
- These high-speed filtration tanks 3 are upward-flow-type filtration tanks, each of which is provided with a vertical rainwater inlet 12 as shown in FIG. Rainwater is supplied from these rainwater inlets 12 to the lower part of the tank, and impurities and SS are captured while passing upward through the packed bed of the floating filter medium 11, and the treated water flows upward.
- each high-speed filtration tank 3 is a common treatment water tank 13, and the treated water flows from its end (the right end in the drawing) to the rainwater treatment water channel 14 and is discharged to rivers, etc. Is done.
- four common treatment water tanks 13 are connected.
- a simple treated water bypass discharge channel is installed at the outlet of the normal primary sedimentation basin, and if this channel is used, it can be converted to a rainwater treated channel.
- a rainwater inflow channel 15 for distributing rainwater to the rainwater inflow section 12 of each of the above-described tanks is formed above the high-speed filtration tank 3.
- the rainwater inflow channel 15 is installed at a high position so that the water level corresponding to the head loss can be secured.
- the height of the weir of the water inflow channel 15 is 0.2 higher than the liquid level of the common treatment water tank 13. Keep at least 1 m higher.
- Rainwater is pumped into the rainwater inflow channel 15 by the rainwater pump 9 or the sewage pump 8 as necessary, and the corresponding high-speed filtration is performed through a plurality of inflow weirs 16 provided in the rainwater inflow channel 15. Rainwater is distributed to the rainwater inlet 1 2 of tank 3 by gravity.
- the total amount of inflow water exceeding Q during rainfall is pumped into the rainwater inflow channel 15 by the rainwater pump 9 or, if necessary, the pump 8.
- the rainwater treatment apparatus of the present invention can handle an inflow water amount greatly exceeding 3 Q (for example, 5 Q to 7 Q), even in the case of abnormal heavy rain, there is a possibility that the treatment capacity may be exceeded. Therefore, a rainwater bypass gate 17 is installed at the end of the rainwater inflow channel 15, for example, to overflow excess rainwater, and the excess rainwater flows down to the rainwater treatment channel 14 and is directly discharged to rivers, etc. It is preferable to be able to do so.
- the height of the rainwater bypass gate 17 can be arbitrarily determined in advance.
- the floating filter medium 11 used in the present invention is preferably made of a foamed polymer having an apparent density of 0.1 to 0.4 and a 50% compression hardness of 0.1 MPa or more.
- the foamed polymer having such physical properties include polypropylene, polystyrene, and polyethylene.
- closed-cell foamed polyethylene having a controlled foaming degree has high heat resistance, chemical resistance, and weather resistance. Is also preferable. If the apparent density of the floating filter medium 11 is less than 0.1, the desired compression hardness cannot be obtained, and the packed layer of the floating filter medium does not easily expand during backwashing. Conversely, if it exceeds 0.4, it may flow downward during backwashing.
- the 50% compression hardness is less than 0.1 MPa, the filter medium will be compacted during high-speed filtration, and it will not be possible to capture a large amount of SS.
- the 50% compression hardness means the pressure required to crush the filter medium to half its height.
- the floating filter medium 11 used in the present invention an irregular or cylindrical one having a size of 4 to 1 Omm is preferable.
- the uneven shape does not mean a simple shape such as a cube or a sphere, but a different shape having some unevenness on the outer surface.
- Such an uneven floating medium 11 has the advantage of forming a large non-linear gap between each other and capturing a large amount of SS.
- the cylindrical and each cylindrical floating filter medium 11 has an advantage that a large amount of SS can be captured similarly.
- FIGS. 7 to 11 show examples of filter media that can be used in the present invention.
- Fig. 7 shows a filter medium with four arms 9
- Fig. 8 shows a filter medium 2 with a wavy concave and convex formed on the outer peripheral surface of a rectangular plate-shaped body
- Fig. 9 shows a cross section Z
- FIG. 10 shows a filter medium on a tube
- FIG. 11 shows a windmill type filter medium in which the blade portion of FIG. 7 is deformed. If the size of the floating filter medium 11 is smaller than 4 mm, it tends to be clogged, so it is not suitable for high-speed filtration. If it exceeds 10 mm, the capture rate of SS decreases.
- the size of the floating filter medium 11 having a different shape means the maximum value of the outer diameter. Note that, in addition to the above-mentioned floating filter medium 11, a spherical filter medium having a smaller apparent density can be filled.
- the high-speed filtration tank 3 filled with such a floating filter medium 11 can capture a large amount of SS without consolidation of the filter medium, and thus can process a large amount of rainwater at high speed.
- a washing drain valve 18 is provided at the bottom of each high-speed filtration tank 3 so that water at the bottom of the tank can be discharged to the washing drain tank 4 via the washing drain pipe 19.
- washing / drain valve 18 of one of the high-speed filtration tanks 3 is opened, the upper common processing The treated water in the 7j tank 13 flows back downward through the high-speed filtration tank 3 having the opened washing / draining valve 18 to backwash the packed bed of the floating filter medium 11. Washing wastewater is guided to a wastewater inflow channel 22 or a conventional first sedimentation basin 1 as shown in FIG. In the present embodiment, the cleaning drainage valve 18 is used. However, the cleaning drainage can be discharged through a siphon type drainage channel without using the cleaning drainage valve 18.
- This equipment is capable of washing the high-speed filtration tank 3 with secondary effluent from the sewage treatment plant (secondary effluent after treatment in the reaction tank) in order to prevent bad smell during shutdown.
- a secondary treated water supply pipe 21 for supplying the secondary treated water to the common treated water tank is provided.
- the combined sewage flowing into the sand settling tank 5 is equal to or less than the design water quantity Q. Therefore, the entire quantity is guided to the conventional first sedimentation basin 1 by the sewage pump 8, and the conventional sewage treatment is performed.
- the rainwater treatment apparatus of the present invention can rapidly filter a large amount of rainwater, and as long as the amount of inflow water does not abnormally increase, even if the amount of rainwater fluctuates, the design water amount Q is exceeded in response to the fluctuation. Every minute can be filtered. Since the SS removal rate of the high-speed filtration tank in the present invention is about 70%, most pollutants can be removed even when a large amount of rainwater exceeding 3 Q flows in, unlike the conventional case. When the rainfall continues, the pressure loss of each high-speed filtration tank 3 gradually increases, but the increase usually varies.
- the pressure loss of each high-speed filtration tank 3 can be known from the difference between the water level of the common treatment water tank 13 and the water level of the rainwater inflow part.However, since the water level of the common treatment water tank 13 is common to each tank, it is the same. Yes, the rise in pressure drop in each tank can be grasped by the rise in water level at the rainwater inflow section.
- Fig. 5 shows this state as an example, and shows that the pressure drop in the leftmost tank has increased and the water level in the rainwater inflow section 12 has risen significantly as compared to the other tanks. As a result, the rainwater inflow level rises to near the water level of the rainwater inflow channel 15, but washing starts automatically when the predetermined filter media pressure loss or the rainwater inflow water level is reached.
- the backwashing is sequentially performed from the high-speed filtration tanks 3 that have reached the above-mentioned automatic cleaning timing pressure loss.
- the backwashing is performed by opening the washing drainage valve 18 at the bottom and flowing the treated water in the common treated water tank 13 downward.
- Figure 6 shows this situation, with the leftmost tank being backwashed.
- the floating filter medium 11 having an apparent density of, for example, 0.1 to 0.4 is used, it is possible to effectively prevent the filter medium from flowing out together with the backwash water.
- the backwash water enters the washing / drainage tank 4 and is guided to the conventional sewage inflow channel 2 or the first settling basin 1 by the drainage pump 20 for treatment. In this way, backwashing is performed naturally only by opening the washing drainage valve 18, and there is no need to operate a washing pump or the like.
- the rainwater continuously flows in from the rainwater inflow section 12, and the high-speed filtration tanks other than the tank to be washed are continuously treated in the common treatment tank 13 because the high-speed filtration process continues. Water is supplied.
- the time required for backwashing in one tank depends on the thickness of the filter media. However, when the thickness of the filter media is 0.5 to lm, it takes about 1 to 2 minutes.
- the second tank from the left may reach the timing of backwashing. In this case, the washing of the leftmost tank is completed, and the second tank from the left is waiting for washing until the water level in the common treated water tank 13 reaches the predetermined level. Become. Even in this case, since the tank continues to be treated, the water level of the rainwater inflow channel 15 and the rainwater inflow section 12 may reach the same level at the highest due to the further increase in pressure loss. In this case, the amount of water treated in this tank is reduced to the amount corresponding to the pressure loss of the filter media in that tank, so the amount of water transferred from the rainwater inflow channel 15 to the rainwater inflow section is reduced compared to other tanks.
- the reduced amount of water flows into the rainwater inflow section 12 of another tank and is treated. Therefore, even if the timing of backwashing happens to coincide, there is no maintenance operation related to rainwater inflow operation. Further, in the present invention, as described above, the cleaning time is about 2 minutes, and the cleaning standby time does not actually pose a problem. As described above, rainwater treatment is continued while performing the above-mentioned backwashing sequentially for the tanks whose pressure loss has risen to the predetermined level. The amount of inflow into the water is regulated naturally.
- the rainwater treatment apparatus of the present invention As described above, according to the rainwater treatment apparatus in the combined sewer system of the present invention and the sewage treatment system using the same, the rainwater inflow exceeding Q that has been conventionally discharged with simple treatment or no treatment is provided. Most of them can be filtered and contribute to the purification of rivers and other environments. Further, the rainwater treatment apparatus of the present invention has an advantage that it is not necessary to construct a new civil engineering structure and secure an installation space since the first sedimentation basin of the combined sewage treatment plant can be sectioned and provided. Furthermore, the rainwater treatment apparatus of the present invention is almost maintenance-free. In particular, since there is no operation to be performed by humans in response to changes in rainfall during rainfall and the flow rate can be adjusted naturally, the management is easy and this is easy.
- the backwashing of each high-speed filtration tank can be performed using the treated water in the common treated water tank without stopping the operation of the entire apparatus.
- the present invention relates to a rainwater treatment apparatus used for sewage treatment of sewerage with sewage and rainwater, and a sewage treatment system using the rainwater treatment apparatus. It has great industrial applicability in that it can be treated and contributes to the purification of rivers and other environments.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtration Of Liquid (AREA)
- Sewage (AREA)
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/343,179 US6821445B2 (en) | 2001-04-04 | 2002-04-04 | Rainwater-treating apparatus in combined sewer system and backwashing method therefor |
DE60226965T DE60226965D1 (de) | 2001-04-04 | 2002-04-04 | Vorrichtung zur regenwasserbehandlung in mischwasserkanälen und zugehöriges verfahren für die rückspülung |
EP02714472A EP1380330B1 (en) | 2001-04-04 | 2002-04-04 | Rain water treating device in combined sewage, and backwashing method therefor |
JP2002579087A JP3824583B2 (ja) | 2001-04-04 | 2002-04-04 | 合流式下水道における雨水処理装置及びその逆洗方法 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001105637 | 2001-04-04 | ||
JP2001-105637 | 2001-04-04 |
Publications (1)
Publication Number | Publication Date |
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WO2002081050A1 true WO2002081050A1 (fr) | 2002-10-17 |
Family
ID=18958292
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2002/003404 WO2002081050A1 (fr) | 2001-04-04 | 2002-04-04 | Dispositif de traitement des eaux de pluie dans des eaux d'egout mixtes et procede de lavage a contre-courant associe |
Country Status (5)
Country | Link |
---|---|
US (1) | US6821445B2 (ja) |
EP (1) | EP1380330B1 (ja) |
JP (1) | JP3824583B2 (ja) |
DE (1) | DE60226965D1 (ja) |
WO (1) | WO2002081050A1 (ja) |
Cited By (6)
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JP2005218991A (ja) * | 2004-02-06 | 2005-08-18 | Unitika Ltd | 合流式下水道におけるろ過処理方法 |
JP2008000697A (ja) * | 2006-06-23 | 2008-01-10 | Ngk Insulators Ltd | 合流式下水の一次処理方法 |
JP2009226332A (ja) * | 2008-03-24 | 2009-10-08 | Metawater Co Ltd | ろ過設備の洗浄方法 |
WO2012105172A1 (ja) * | 2011-02-02 | 2012-08-09 | メタウォーター株式会社 | ろ過システム |
JP2017177028A (ja) * | 2016-03-31 | 2017-10-05 | 株式会社システック | ろ過材及びこれを用いたろ過装置及びろ過材の閉塞回避方法 |
CN108993022A (zh) * | 2018-08-10 | 2018-12-14 | 浙江顺艺园林工程有限公司 | 一种市政雨水收集回收利用系统 |
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DE20103875U1 (de) * | 2001-03-07 | 2001-08-16 | Vollmar Gmbh | Abwasseranlage mit Reinigungsvorrichtung |
US7052206B1 (en) * | 2003-04-30 | 2006-05-30 | Mastromonaco Ralph G | System and method for use of an extention basin as a storm water control device |
FR2879943B1 (fr) * | 2004-12-23 | 2007-07-13 | Sources Sa | Plancher-support destine a la filtration d'eaux usees et cellules de traitement comportant un tel plancher-support |
FR2880549B1 (fr) * | 2004-12-29 | 2007-03-16 | Sources Sa | Cellule de traitement destinee a la filtration d'eaux usees et comportant un deflecteur anti-perte de materiau |
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US20060289358A1 (en) * | 2005-06-22 | 2006-12-28 | Geospec, Inc. | Methods and apparatus for removing contaminants from storm water |
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CN108744709B (zh) * | 2018-06-29 | 2020-12-29 | 吉林省拓维环保集团股份有限公司 | 一种新型工业废水处理池 |
US11980835B2 (en) * | 2020-07-27 | 2024-05-14 | Foley Products Company, Llc | Double-filter basket for stormwater retention system drain |
KR102327003B1 (ko) * | 2021-01-15 | 2021-11-16 | 주식회사 부강테크 | 하·폐수의 1차 처리, 유량 조절 및 초기 우수 처리가 가능하며 고속여과를 포함하는 침전조 |
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JPH05317841A (ja) * | 1992-04-09 | 1993-12-03 | Hitachi Plant Eng & Constr Co Ltd | 下水処理施設 |
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JPS6224910A (ja) | 1985-07-19 | 1987-02-02 | Sanwa Daiyamondo Kogyo Kk | 硬質物切削用帯のこ |
US5317841A (en) * | 1992-08-28 | 1994-06-07 | Whitemetal, Inc. | Method for removal of surface contaminants from metal substrates |
US5558763A (en) * | 1993-06-24 | 1996-09-24 | Hitachi Plant Engineering & Construction Co., Ltd. | Sewage treatment system with air jetting means |
DE19511008C2 (de) * | 1995-03-25 | 2000-09-28 | Vsb Vogelsberger Umwelttechnis | Siebanordnung für kreisförmige Regenwasserentlastungsanlagen |
DE19820259C2 (de) * | 1998-05-06 | 2000-08-24 | Dieter Kruse | Vorrichtung zum Reinigen, Spülen und Waschen eines Abwasserstromes in einem Zulaufgerinne einer Kläranlage |
UA69413C2 (uk) * | 1998-05-22 | 2004-09-15 | Брістол-Майерс Сквібб Компані | Фармацевтична композиція, яка містить серцевину та ентеросолюбільну оболонку, фармацевтична композиція у вигляді сфероїдальних гранул, спосіб одержання сфероїдальних гранул та спосіб одержання фармацевтичної композиції |
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2002
- 2002-04-04 EP EP02714472A patent/EP1380330B1/en not_active Expired - Lifetime
- 2002-04-04 DE DE60226965T patent/DE60226965D1/de not_active Expired - Lifetime
- 2002-04-04 JP JP2002579087A patent/JP3824583B2/ja not_active Expired - Lifetime
- 2002-04-04 WO PCT/JP2002/003404 patent/WO2002081050A1/ja active IP Right Grant
- 2002-04-04 US US10/343,179 patent/US6821445B2/en not_active Expired - Lifetime
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JPH05317841A (ja) * | 1992-04-09 | 1993-12-03 | Hitachi Plant Eng & Constr Co Ltd | 下水処理施設 |
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Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2005218991A (ja) * | 2004-02-06 | 2005-08-18 | Unitika Ltd | 合流式下水道におけるろ過処理方法 |
JP2008000697A (ja) * | 2006-06-23 | 2008-01-10 | Ngk Insulators Ltd | 合流式下水の一次処理方法 |
JP4674188B2 (ja) * | 2006-06-23 | 2011-04-20 | メタウォーター株式会社 | 合流式下水の一次処理方法 |
JP2009226332A (ja) * | 2008-03-24 | 2009-10-08 | Metawater Co Ltd | ろ過設備の洗浄方法 |
WO2012105172A1 (ja) * | 2011-02-02 | 2012-08-09 | メタウォーター株式会社 | ろ過システム |
JP2012157842A (ja) * | 2011-02-02 | 2012-08-23 | Metawater Co Ltd | ろ過システム |
US10407317B2 (en) | 2011-02-02 | 2019-09-10 | Metawater Co., Ltd. | Floating filter media filtration system with backwash |
JP2017177028A (ja) * | 2016-03-31 | 2017-10-05 | 株式会社システック | ろ過材及びこれを用いたろ過装置及びろ過材の閉塞回避方法 |
CN108993022A (zh) * | 2018-08-10 | 2018-12-14 | 浙江顺艺园林工程有限公司 | 一种市政雨水收集回收利用系统 |
CN108993022B (zh) * | 2018-08-10 | 2021-08-10 | 浙江顺艺园林工程有限公司 | 一种市政雨水收集回收利用系统 |
Also Published As
Publication number | Publication date |
---|---|
EP1380330A1 (en) | 2004-01-14 |
JP3824583B2 (ja) | 2006-09-20 |
US6821445B2 (en) | 2004-11-23 |
US20030106859A1 (en) | 2003-06-12 |
JPWO2002081050A1 (ja) | 2004-07-29 |
EP1380330B1 (en) | 2008-06-04 |
EP1380330A4 (en) | 2004-12-08 |
DE60226965D1 (de) | 2008-07-17 |
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