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JP5062138B2 - Cleaning method for air diffuser - Google Patents

Cleaning method for air diffuser Download PDF

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JP5062138B2
JP5062138B2 JP2008272923A JP2008272923A JP5062138B2 JP 5062138 B2 JP5062138 B2 JP 5062138B2 JP 2008272923 A JP2008272923 A JP 2008272923A JP 2008272923 A JP2008272923 A JP 2008272923A JP 5062138 B2 JP5062138 B2 JP 5062138B2
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air
diffuser
water
cleaning
supply
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JP2009172575A (en
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雅則 長藤
一聡 大橋
稔 山本
猛志 辻
至 坂井
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JFE Engineering Corp
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • B01F23/23105Arrangement or manipulation of the gas bubbling devices
    • B01F23/2312Diffusers
    • B01F23/23128Diffusers having specific properties or elements attached thereto
    • B01F23/231281Diffusers having specific properties or elements attached thereto made of or comprising a biocide
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/20Activated sludge processes using diffusers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • B01F23/23105Arrangement or manipulation of the gas bubbling devices
    • B01F23/2311Mounting the bubbling devices or the diffusers
    • B01F23/23114Mounting the bubbling devices or the diffusers characterised by the way in which the different elements of the bubbling installation are mounted
    • B01F23/231143Mounting the bubbling elements or diffusors, e.g. on conduits, using connecting elements; Connections therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • B01F23/23105Arrangement or manipulation of the gas bubbling devices
    • B01F23/2312Diffusers
    • B01F23/23123Diffusers consisting of rigid porous or perforated material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • B01F23/23105Arrangement or manipulation of the gas bubbling devices
    • B01F23/2312Diffusers
    • B01F23/23123Diffusers consisting of rigid porous or perforated material
    • B01F23/231231Diffusers consisting of rigid porous or perforated material the outlets being in the form of perforations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • B01F23/23105Arrangement or manipulation of the gas bubbling devices
    • B01F23/2312Diffusers
    • B01F23/23124Diffusers consisting of flexible porous or perforated material, e.g. fabric
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • B01F23/23105Arrangement or manipulation of the gas bubbling devices
    • B01F23/2312Diffusers
    • B01F23/23126Diffusers characterised by the shape of the diffuser element
    • B01F23/231262Diffusers characterised by the shape of the diffuser element having disc shape
    • 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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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Cleaning By Liquid Or Steam (AREA)
  • Detergent Compositions (AREA)
  • Activated Sludge Processes (AREA)

Description

本発明は、散気装置の洗浄方法に関し、特に、散気板の散気面に付着した汚れ成分を確実に除去できる散気装置の洗浄方法に関する。   The present invention relates to a method for cleaning an air diffuser, and more particularly, to a method for cleaning an air diffuser that can reliably remove dirt components attached to an air diffuser surface of an air diffuser plate.

下水処理施設において汚水中の窒素化合物や炭素化合物を除去するために、微生物による分解、吸着作用を利用した活性汚泥法が用いられている。活性汚泥中の微生物が活動するためには微生物に酸素を与える必要がある。散気装置は、下水処理施設の曝気槽の底部等に設置されて水中に酸素を供給する装置である。散気装置には、散気面が膜タイプの散気装置(特許文献1)と、散気面が金属薄板タイプの散気装置(特許文献2)が存在する。金属薄板タイプの散気装置は、散気による圧損が少なく、かつ耐久性および保守点検の容易性において優れている。   In order to remove nitrogen compounds and carbon compounds in sewage at a sewage treatment facility, an activated sludge method utilizing decomposition and adsorption by microorganisms is used. In order for the microorganisms in the activated sludge to be active, it is necessary to give oxygen to the microorganisms. The air diffuser is an apparatus that is installed at the bottom of an aeration tank of a sewage treatment facility and supplies oxygen into water. There are two types of diffusers: a diffuser with a film diffuser surface (Patent Document 1) and a diffuser with a metal thin plate type diffuser surface (Patent Document 2). The thin metal plate type air diffuser has less pressure loss due to air diffused, and is excellent in durability and ease of maintenance and inspection.

散気装置は、長期間にわたって曝気運転を継続すると、汚れ成分が膜または金属薄板の微細孔の内部および表面に付着して目詰まりを起こす。目詰まりを起こす汚れ成分の多くは微生物により形成されるスライムであり、これが散気孔を閉塞させる。このスライムの付着力は強く、ガス圧を高めてもスライムを剥離することはできない。   When the aeration apparatus continues aeration operation for a long period of time, the dirt component adheres to the inside and the surface of the fine holes of the film or the metal thin plate, thereby causing clogging. Most of the soil components that cause clogging are slimes formed by microorganisms, which block the air holes. The slime has a strong adhesive force, and the slime cannot be peeled off even if the gas pressure is increased.

膜タイプの散気装置では、散気装置の送気操作によってメンブランを伸長または収縮させ、膜の微細孔の内部および表面に付着した微生物由来のスライムを取り除く方法が開示されている(特許文献3)。   In the membrane-type air diffuser, a method is disclosed in which the membrane is elongated or contracted by the air-feeding operation of the air diffuser to remove the microorganism-derived slime attached to the inside and the surface of the micropores of the membrane (Patent Document 3). ).

しかし、金属薄板タイプの散気装置では、散気面が伸縮性のない剛体であるため、上述したような目詰まり防止処置を施すことはできない。現状では、金属薄板タイプの散気装置において微生物が増殖して目詰まりが発生した場合には、散気装置を水面上に引き上げて散気薄板を清掃しなければならず、散気装置の維持管理に多大な労力と費用を要する。   However, in the thin metal plate type air diffuser, since the air diffused surface is a rigid body having no elasticity, the above-described clogging prevention treatment cannot be performed. At present, when clogging occurs due to the growth of microorganisms in a thin metal plate type diffuser, the diffuser plate must be cleaned by lifting the diffuser onto the water surface. Management requires a lot of labor and expense.

また、膜タイプおよび金属薄板タイプの両方において、酸素移動効率を高めるために散気面の気孔径を小さくする必要があるが、気孔径が小さくなればなるほど目詰まりが起こりやすくなる。目詰まりの起こりやすい散気装置は、水面上に引き上げて散気薄板を頻繁に清掃しなければならない。
特開2003−320388号公報 特開2006−61817号公報 特開2004−313938号公報
In both the membrane type and the thin metal plate type, it is necessary to reduce the pore diameter of the diffuser surface in order to increase the oxygen transfer efficiency. However, the smaller the pore diameter, the more likely clogging occurs. Air diffusers that are prone to clogging must be lifted above the surface of the water and frequently cleaned.
JP 2003-320388 A JP 2006-61817 A JP 2004-313938 A

このように、従来の散気装置は、目詰まりの問題に対して十分な解決手段を備えていなかった。
そこで、本発明においては、長期間の使用により散気面に目詰まりが生じた場合において、散気面が伸縮性のない剛体である散気板に対しても、散気板を水面に引き上げて清掃することなく、散気面の目詰まりの解消をできる散気装置の洗浄方法を提供することを目的としている。
Thus, the conventional diffuser has not been provided with a sufficient solution to the clogging problem.
Therefore, in the present invention, when the diffuser surface is clogged due to long-term use, the diffuser plate is pulled up to the water surface even with respect to the diffuser plate which is a rigid body having no elasticity. It is an object of the present invention to provide a cleaning method for an air diffuser that can eliminate clogging of the air diffuser surface without cleaning.

発明者は上記の課題を解決するために、水あるいは薬液などの洗浄水等を散気用給気配管内に注入し、これを散気用の空気によって散気板側に供給することによって散気板に付着したスライム(バイオフィルム)を自動洗浄することを考えた。そして、これを実現するためにための具体的手段として、一端が散気板に連通し、他端が散気用給気配管に内挿入される内挿管を設け、この内挿管を介して洗浄水を散気板に供給して水ブローすることを考えた。   In order to solve the above-mentioned problem, the inventor injects water or cleaning water such as a chemical solution into the air supply pipe for air diffusion, and supplies the air to the air diffusion plate side with air for air diffusion. We considered automatic cleaning of slime (biofilm) adhering to the plate. As a specific means for realizing this, an internal intubation is provided in which one end communicates with the air diffuser plate and the other end is inserted into the air supply pipe for air diffusion, and cleaning is performed via the internal intubation. We considered supplying water to the diffuser and blowing water.

しかし、何らかの要因で散気板にバイオフィルムが完全に付着した場合は、水ブローでのバイオフィルムの完全な除去は困難であり、酸素移動効率の低下と散気装置の圧力損失の上昇による曝気動力が設置当初より大となることが避けられない。
そこで、発明者は散気板の散気孔壁面に付着したバイオフィルムを効果的に除去する方法として、散気板に形成されたバイオフィルムを化学的に分解して除去することを検討したところ、バイオフィルムの除去にはアルカリが有効であることが判明した。これは、バイオフィルムは微生物の塊で、たんぱく質が主成分であり、アルカリがたんぱく質を溶かすためである。
However, if the biofilm completely adheres to the diffuser plate for some reason, it is difficult to completely remove the biofilm by water blow, and aeration due to a decrease in oxygen transfer efficiency and an increase in the pressure loss of the diffuser. It is inevitable that the power will be greater than the initial installation.
Therefore, the inventor examined the removal of the biofilm formed on the diffuser plate by chemically decomposing it as a method of effectively removing the biofilm attached to the diffuser wall of the diffuser plate. It has been found that alkali is effective in removing biofilms. This is because the biofilm is a mass of microorganisms, the protein is the main component, and the alkali dissolves the protein.

ところで、水ブローの場合にはスライムを物理的に除去するものであり、ブロー時間も数分程度で済む。
一方、アルカリにてたんぱく質を分解除去することは化学反応であり、時間をある程度かける必要がある。また、この分解作用時間においては、散気面に曝気槽内の汚水が逆流しないように、常に散気用給気配管(ヘッダ管)内が曝気槽汚水の圧力に対して正圧を維持するようにしなければならない。汚水が逆流すると、散気板に汚水中のアルミニウムなどの金属塩とアルカリが反応し、固形物を析出し、散気板の開孔に目詰まりを起こすからである。
By the way, in the case of water blow, the slime is physically removed, and the blow time is only a few minutes.
On the other hand, decomposing and removing proteins with alkali is a chemical reaction and requires some time. In addition, during this decomposition action time, the inside of the aeration tank (header pipe) always maintains a positive pressure with respect to the pressure of the aeration tank sewage so that the sewage in the aeration tank does not flow back to the diffusion surface. Must do so. This is because when the sewage flows backward, a metal salt such as aluminum in the sewage reacts with the alkali on the diffuser plate to precipitate solids and clogs the openings of the diffuser plate.

このような逆流を防止してアルカリ液を注入する方法として、アルカリ液を酸気用給気配管(ヘッダ管)内に満管になるまで注入し、かつ、アルカリがバイオフィルムを分解作用する30分間程度の間、アルカリ液を常時供給することが考えられる。
しかしながら、この方法ではアルカリ液はバイオフィルムを分解するのに必要な量に対して、過大な量を注入しなければならないので、経済的でなく、また曝気槽に多量のアルカリが混入するので、活性汚泥への悪影響が懸念される。
そこで、発明者はこの問題を解決するために鋭意検討した結果、散気用給気配管(ヘッダ管)内にアルカリ液を必要な量だけ注入した後に、密閉状態の散気用給気配管内に微量の空気を連続注入することにより、この空気圧によって散気用給気配管(ヘッダ管)内に貯留されたアルカリ液を内挿管を介して散気板に時間をかけて押し出し供給することができるとの知見を得た。
本発明はかかる知見に基づきなされたものであり、具体的には以下のような構成を有するものである。
As a method of injecting the alkaline liquid while preventing such a backflow, the alkaline liquid is injected into the acid supply pipe (header pipe) until it becomes full, and the alkali decomposes the biofilm 30. It is conceivable to always supply the alkaline solution for about a minute.
However, in this method, an excessive amount of alkali solution must be injected relative to the amount necessary to decompose the biofilm, which is not economical and a large amount of alkali is mixed in the aeration tank. There are concerns about the negative impact on activated sludge.
Therefore, as a result of intensive studies to solve this problem, the inventor injected a required amount of alkaline liquid into the air supply pipe (header pipe) for air diffusion, and then into the air supply pipe for air diffusion in the sealed state. By continuously injecting a small amount of air, the alkaline liquid stored in the air supply pipe (header pipe) for air diffusion can be pushed out and supplied to the air diffuser plate via the intubation tube over time. And gained knowledge.
The present invention has been made based on such findings, and specifically has the following configuration.

(1)本発明に係る散気装置の洗浄方法は、曝気槽に設置される微細気孔を有する散気板と、該散気板に接続された散気用給気配管と、該散気用給気配管に開閉弁を介して接続されて該散気用給気配管に散気用空気を供給する給気装置と、一端が前記散気板に連接され、他端が前記散気用給気配管内に内挿された内挿管とを備えた散気装置の洗浄方法であって、
前記散気用給気配管に加圧空気を注入する加圧空気供給装置と、前記散気用給気配管に洗浄薬液を注入する薬液注入装置とを設け、
前記開閉弁を閉止して散気用給気配管に対する前記散気用空気の給気を停止した後、前記薬液注入装置によって洗浄液を前記散気用給気配管内へ供給する洗浄液供給工程と、前記加圧空気供給装置によって前記散気用給気配管内へ加圧空気を30分〜数時間継続して供給し、前記散気用給気配管内の洗浄液を前記内挿管を介して散気板から継続して排出させる散気板薬液洗浄工程を備えたことを特徴とするものである。
(1) A method of cleaning an air diffuser according to the present invention includes an air diffuser plate having fine pores installed in an aeration tank, an air supply pipe for air diffuser connected to the air diffuser plate, and the air diffuser. An air supply device connected to the air supply pipe via an open / close valve to supply air for air supply to the air supply pipe for air diffusion, one end connected to the air diffusion plate, and the other end to the air supply for air diffusion A method of cleaning an air diffuser comprising an intubation inserted in an air pipe,
A pressurized air supply device for injecting pressurized air into the air supply pipe for air diffusion, and a chemical liquid injection device for injecting a cleaning chemical into the air supply pipe for air diffusion,
After stopping the supply of the air diffuser for air to air air supply piping scattered by closing the on-off valve, the cleaning agent liquid supply for supplying a cleaning agent liquid feeding to sign tube for the air diffuser by the liquid injector a step, and continuously supplied to the pressurized air supply device by said air diffuser for supply to the sign tube pressurized air 30 minutes to several hours, through the intubation cleaning agent liquid of the air diffuser for supply quotations tube further comprising a diffuser plate chemical cleaning process of discharging continuously dispersed from the vapor plate Te is characterized in.

(2)また、上記(1)に記載のものにおいて、散気用給気配管内にブロー水を供給するブロー水供給手段を設け、洗浄液による洗浄後、前記ブロー水供給手段によって散気用給気配管内にブロー水を供給すると共に散気用給気配管内に散気用空気を送風して該ブロー水を内挿管を介して散気板に供給して水ブローする水ブロー工程を備えたことを特徴とするものである。
(2) Further, in those described in the above (1), provided with a blowing water supply means for supplying blow water supply quotations tube for aeration, after washing with the washing agent solution, for air diffuser by the blow water supplier It has a water blow process for supplying blow water into the air supply pipe and blowing air into the air supply pipe for supplying air and supplying the blow water to the air diffuser plate through the intubation to blow water. It is characterized by this.

(3)また、上記(2)に記載のものにおいて、洗浄液が、アルカリを主成分とした薬液であることを特徴とするものである。
(3) Further, in those described in the above (2), cleaning agent liquid is characterized in that a chemical solution composed mainly of an alkali.

(4)また、上記(3)に記載のものにおいて、洗浄液が、炭酸ナトリウムを含有することを特徴とするものである。 (4) In those described in the above (3), irrigant fluid, it is characterized in that it contains sodium carbonate.

本発明の散気装置の洗浄方法によれば、散気板を水面に引き上げて清掃することなく、散気板に付着したバイオフィルムを効果的に除去して、散気板の目詰まりを解消することができる。   According to the method for cleaning an air diffuser of the present invention, the biofilm adhered to the air diffuser is effectively removed without lifting the air diffuser to the surface of the water, and the clogging of the air diffuser is eliminated. can do.

以下、本発明の実施の形態を図面に基づいて説明する。   Hereinafter, embodiments of the present invention will be described with reference to the drawings.

1.散気装置
図1は、本実施の形態に係る散気装置を示す模式図である。本実施の形態においては、洗浄液として、アルカリを主成分とする薬液(以下、「アルカリ液」という)を用いる場合を例に挙げて説明する。
本実施の形態の散気装置1は、ガス供給手段2とガス供給手段2から供給される空気を散気板へと導く散気用給気配管3(ヘッダ管)と、散気用給気配管3から散気用空気の供給を受けて微細気泡を放出する散気板4と、上端が散気板4に連接され、下端が前記散気用給気配管3内に内挿された内挿管7と、薬液注入管13を介して散気用給気配管3にアルカリ液を注入する薬液注入装置14と、空気注入管15を介して散気用給気配管3に加圧空気を注入する加圧空気供給装置16と、ブロー水供給管17を介して散気用給気配管3にブロー水を供給するブロー水供給手段5とを備えている。
1. Air diffuser FIG. 1 is a schematic diagram showing an air diffuser according to the present embodiment. In the present embodiment, a case where a chemical liquid containing alkali as a main component (hereinafter referred to as “alkaline liquid”) is used as an example of the cleaning liquid will be described.
The air diffuser 1 according to the present embodiment includes a gas supply means 2, an air supply pipe 3 (header pipe) for guiding air supplied from the gas supply means 2 to an air diffuser plate, and an air supply for air diffusion. A diffuser plate 4 that receives supply of air for aeration from the pipe 3 and releases fine bubbles, an upper end connected to the aeration plate 4, and a lower end inserted into the aeration air supply pipe 3. Pressurized air is injected into the air supply pipe 3 through the intubation 7, the chemical liquid injection device 14 that injects the alkaline liquid into the air supply pipe 3 through the chemical liquid injection pipe 13, and the air supply pipe 3 through the air injection pipe 15. And a blow water supply means 5 for supplying blow water to the air supply pipe 3 for diffusion through a blow water supply pipe 17.

散気用給気配管3には開閉弁18が、また薬液注入管13には開閉弁19が、さらに空気注入管15には開閉弁20が、またさらにブロー水供給管17には開閉弁21がそれぞれ設けられている。
以下、散気装置1の主な構成について詳細に説明する。
An opening / closing valve 18 is provided in the air supply piping 3, an opening / closing valve 19 is provided in the chemical solution injection pipe 13, an opening / closing valve 20 is provided in the air injection pipe 15, and an opening / closing valve 21 is provided in the blow water supply pipe 17. Are provided.
Hereinafter, the main configuration of the air diffuser 1 will be described in detail.

<散気板>
散気板4は、膜タイプまたは金属薄板タイプなど、いかなる形態の散気板であってもよい。例えば、散気板4が金属薄板タイプの場合、機械加工によって形成した微細孔またはスリットを有する金属薄板が用いられる。
ガス供給手段2より供給された空気は、散気用給気配管3から内挿管7を通して散気板4に送気され、散気板4の散気面に点在する複数の散気孔から放出される。
<Air diffuser>
The diffuser plate 4 may be any form of diffuser plate such as a membrane type or a thin metal plate type. For example, when the diffuser plate 4 is a thin metal plate type, a thin metal plate having fine holes or slits formed by machining is used.
The air supplied from the gas supply means 2 is supplied to the diffuser plate 4 from the diffuser supply pipe 3 through the inner tube 7 and discharged from a plurality of diffuser holes scattered on the diffuser surface of the diffuser plate 4. Is done.

<内挿管>
本実施形態における散気装置1は、内挿管7を備えているために、散気用給気配管3を水で満管にしなくても水を散気板4の散気孔に供給して水ブローすることができる。従って、大量の水は必要とせず、特に、抗菌物質を含む水溶液を供給する場合は、少ない抗菌物質で短時間かつ効率的に微生物を除去することができる。この結果、散気板4へのバイオフィルムの付着を防止でき、薬液洗浄の回数を少なくできるので、散気装置を水面下で長期かつ安定的に運転することができる。
<Intubation>
Since the air diffuser 1 according to the present embodiment includes the inner intubation tube 7, water is supplied to the air diffuser holes of the air diffuser plate 4 without filling the air diffuser air supply pipe 3 with water. Can blow. Therefore, a large amount of water is not required. In particular, when an aqueous solution containing an antibacterial substance is supplied, microorganisms can be efficiently removed in a short time with a small amount of the antibacterial substance. As a result, the biofilm can be prevented from adhering to the diffuser plate 4 and the number of times of chemical cleaning can be reduced, so that the diffuser can be operated stably for a long time under the surface of the water.

なお、内挿管7が無い場合において、散気板4を水ブローするための水を供給しようとすると、前述のように散気用給気配管3を満水にする必要があるだけでなく、満水にした水を抜くための工夫が必要となる。仮に、水を抜くための手段が無い場合には、散気板4が取り付けられている散気用給気配管内に水が残留し、管路が細くなってしまい、適切な散気ができなくなる。   In the case where there is no internal intubation 7, when trying to supply water for blowing the air diffuser plate 4, it is not only necessary to fill the air supply pipe 3 for air diffusion as described above, It is necessary to devise in order to drain water. If there is no means for draining water, water remains in the air supply piping for the air diffuser to which the air diffuser plate 4 is attached, the pipe line becomes thin, and appropriate air diffusion cannot be performed. .

図2は、内挿管7の一例を示す断面図である。内挿管7は、上端が散気板4に連接され、下端が散気用給気配管3内の底面近傍まで延出するように内挿され、下端部には傾斜した吸い込み面8を有している。   FIG. 2 is a cross-sectional view showing an example of the intubation tube 7. The inner insertion tube 7 has an upper end connected to the diffuser plate 4, and a lower end is inserted so as to extend to the vicinity of the bottom surface in the air supply pipe 3 for diffusion, and has an inclined suction surface 8 at the lower end. ing.

内挿管7は、空気の散気板4への供給路であるとともに、水ブロー処理中は供給されたブロー水を散気板4から排出する機能を有している。   The internal intubation 7 is a supply path to the air diffusion plate 4 and has a function of discharging the supplied blow water from the diffusion plate 4 during the water blowing process.

内挿管7は、散気用給気配管3と一体に形成しても、着脱可能な別部材としてもよい。着脱可能な別部材とする場合、内挿管7は、散気用給気配管3に予め設けた挿入口に挿入して固定することができる。内挿管7の固定方法には、特に制限はなく、あらゆる固定方法が含まれる。例えば、内挿管の側面に固定用締付け部材10を予め溶接し、散気用給気配管側に取付ブラケット11を予め溶接しておくことにより、内挿管7をねじ込んで散気用給気配管3に固定することができる。同様に、散気板4も内挿管7と着脱可能とすることができる。また、内挿管7の材質には、特に制限はなく、好ましくは、プラスチックまたはステンレス鋼、チタン等の金属から形成される。   The inner intubation 7 may be formed integrally with the air supply pipe 3 for diffusing or may be a separate member that can be attached and detached. When it is set as another member which can be attached or detached, the inner intubation tube 7 can be inserted and fixed in the insertion port previously provided in the air supply piping 3 for aeration. There is no restriction | limiting in particular in the fixing method of the intubation tube 7, All fixing methods are included. For example, the fixing tightening member 10 is pre-welded to the side surface of the intubation tube, and the mounting bracket 11 is pre-welded to the air supply piping side, thereby screwing the internal insertion tube 7 into the air supply piping 3 for the air diffusion. Can be fixed to. Similarly, the diffuser plate 4 can be attached to and detached from the inner intubation 7. Moreover, there is no restriction | limiting in particular in the material of the intubation tube 7, Preferably, it forms from metals, such as plastic or stainless steel, titanium.

内挿管7の下端部は吸込み面8を備えている。散気用給気配管3には複数個の散気板4が設置されているが、散気用給気配管3は必ずしも水平に設置されているとは限らず、内挿管7の下端が水面に対して同じ高さに配置されない場合がある。図3に示したように、内挿管下端の吸込み面8が傾斜していない場合は、下端部が水面に接するか水面下にある内挿管7からしか吸い上げ又は押し上げが起こらないため、全ての散気板4にブロー水が均一に供給されず、ブロー水が供給されない一部の散気板で目詰まりが進行する恐れがある。
一方、図4に示したように、内挿管下端の吸込み面8が傾斜している場合は、水面が吸込み面8の上端と下端の間にあればブロー水を吸い上げ可能であり、水面に対する内挿管下端の配置に上下が生じた場合でも、一定範囲であれば全ての内挿管からの吸い上げが可能であり、散気板4に均一なブローが可能である。したがって、吸込み面8が傾斜している場合は、散気用給気配管3の水平方向の設置精度の許容範囲が大きくなる。
The lower end portion of the inner intubation 7 has a suction surface 8. A plurality of diffuser plates 4 are installed in the diffuser supply pipe 3, but the diffuser supply pipe 3 is not necessarily installed horizontally, and the lower end of the intubation pipe 7 is the water surface. May not be arranged at the same height. As shown in FIG. 3, when the suction surface 8 at the lower end of the intubation tube is not inclined, suction or push-up occurs only from the inner intubation tube 7 that is in contact with the water surface or under the water surface. Blow water is not uniformly supplied to the air plate 4, and there is a possibility that clogging may proceed with some diffuser plates to which no blow water is supplied.
On the other hand, as shown in FIG. 4, when the suction surface 8 at the lower end of the intubation tube is inclined, the blow water can be sucked up if the water surface is between the upper end and the lower end of the suction surface 8. Even if the lower end of the intubation is arranged up and down, it can be sucked up from all the inner intubations within a certain range, and uniform blow to the diffuser plate 4 is possible. Therefore, when the suction surface 8 is inclined, the allowable range of the installation accuracy in the horizontal direction of the air supply pipe 3 for air diffusion becomes large.

また、図4に示すように、水位が吸込み面8の上端と下端の間にある場合はブロー速度の大きい気水混相のブローとなるが、図5に示すように水位が吸込み面8より高くなった場合は、水だけを押し上げるため、空気が混相しない水押出しブローとなる。   As shown in FIG. 4, when the water level is between the upper end and the lower end of the suction surface 8, the air / water mixed phase is blown at a high blow speed, but the water level is higher than the suction surface 8 as shown in FIG. In this case, since only water is pushed up, the water extrusion blow does not mix the air.

傾斜した吸い込み面8の下端は、散気用給気配管3の内底近傍に位置し、たとえ水位が低くても、確実にブロー水を内挿管7内に吸い上げ又は押し上げることができるようにする。傾斜した吸い込み面8の下端は、散気用給気配管3の内底より0〜10mm上方にあることが好ましい。
傾斜した吸い込み面8の垂直方向に対する傾斜角度θに特に制限はないが、内挿管7は空気の供給路でもあるため、空気を十分に内挿管7内に送気できるような傾斜角度θにすることが好ましい。傾斜角度θは、例えば10〜85度、好ましくは30〜80度とすることができる。
The lower end of the inclined suction surface 8 is located in the vicinity of the inner bottom of the air supply pipe 3 for air diffusion so that even if the water level is low, the blow water can be surely sucked up or pushed up into the inner intubation tube 7. . The lower end of the inclined suction surface 8 is preferably 0 to 10 mm above the inner bottom of the air supply pipe 3 for air diffusion.
Although there is no particular limitation on the inclination angle θ of the inclined suction surface 8 with respect to the vertical direction, since the intubation tube 7 is also an air supply path, the inclination angle θ is such that air can be sufficiently supplied into the intubation tube 7. It is preferable. The inclination angle θ can be, for example, 10 to 85 degrees, preferably 30 to 80 degrees.

なお、上記の説明では、内挿管7の管壁に通気孔を設けていない例を示したが、これは管壁に通気孔があると、薬液による散気板洗浄の際に通気孔から薬液が漏れて散気板4側へ薬液が供給されないからである。の供給効率が悪くなるからである。
もっとも、内挿管7の管壁に通気孔があっても、薬液による散気板洗浄の際に通気孔の高さ以上になるように薬液を入れるようにすればよいので、内挿管7の管壁に通気孔を設けることを排除するものではない。
In the above description, an example in which a vent hole is not provided in the tube wall of the intubation tube 7 is shown. However, if there is a vent hole in the tube wall, the chemical solution is removed from the vent hole during cleaning of the diffuser plate with the chemical solution. This is because the chemical liquid is not supplied to the diffuser plate 4 side. This is because the supply efficiency of the is deteriorated.
However, even if there is a vent hole in the tube wall of the inner tube 7, it is only necessary to put the chemical solution so as to be higher than the height of the vent hole when cleaning the diffuser plate with the chemical solution. It does not exclude the provision of ventilation holes in the wall.

<ブロー水供給手段>
ブロー水供給手段5はブロー水供給管17を介して散気用給気配管3にブロー水を供給する装置であって、散気用給気配管3の空気圧に打ち勝ってブロー水を散気用給気配管3内に供給できるようになっている。ブロー水供給手段5としては、例えば水等を貯留する貯留槽に、該貯留槽に貯留された水等を送り出す送水ポンプを設けたものがある。
ブロー水供給手段5より供給されるブロー水は、ブロー水供給管17を介して散気用給気配管3に流れ込み、散気用給気配管3から内挿管7を通して散気板4に送水され、空気と同様、散気板4の散気面に点在する複数の散気孔から放出される。
<Blow water supply means>
The blow water supply means 5 is a device for supplying blow water to the air supply pipe 3 through the blow water supply pipe 17 for overcoming the air pressure of the air supply pipe 3 to diffuse the blow water. The air supply pipe 3 can be supplied. As the blow water supply means 5, for example, a storage tank that stores water or the like is provided with a water supply pump that sends out water or the like stored in the storage tank.
The blow water supplied from the blow water supply means 5 flows into the air supply pipe 3 through the blow water supply pipe 17 and is sent from the air supply pipe 3 to the air diffuser plate 4 through the inner tube 7. Like air, the air is emitted from a plurality of air holes scattered on the air diffusion surface of the air diffusion plate 4.

<薬液注入装置>
薬液注入装置14は、薬液注入管13を介して散気用給気配管3にアルカリ液を注入する装置である。薬液注入装置14は、アルカリ液を貯留する貯留槽と貯留槽内のアルカリ液を薬液注入管13に送り出す送液ポンプを備えている。
<Chemical liquid injection device>
The chemical liquid injector 14 is an apparatus that injects an alkaline liquid into the air supply pipe 3 for diffusion through the chemical liquid injector 13. The chemical liquid injector 14 includes a storage tank that stores the alkaline liquid and a liquid feed pump that sends the alkaline liquid in the storage tank to the chemical liquid injection pipe 13.

<加圧空気供給装置>
加圧空気供給装置16は、空気注入管15を介して散気用給気配管3に加圧空気を注入する装置であり、例えばエアポンプから構成される。
<Pressurized air supply device>
The pressurized air supply device 16 is a device that injects pressurized air into the air supply pipe 3 for air diffusion through the air injection pipe 15 and is constituted by, for example, an air pump.

上記のように構成された本実施の形態に係る散気装置1の動作を、散気運転、水ブロー運転、薬液による洗浄に分けて説明する。
<散気運転>
散気運転は、ガス供給手段2から送風される空気を、散気用給気配管3に送り出し、この空気を内挿管7を介して散気板4の微細孔またはスリットから曝気槽12内へ微細気泡として放出する運転である。散気運転時には、開閉弁18を開放し、開閉弁19、20、21を閉止して運転する。
The operation of the air diffuser 1 according to the present embodiment configured as described above will be described separately for the air diffuser operation, the water blow operation, and the cleaning with the chemical solution.
<Aeration operation>
In the aeration operation, air blown from the gas supply means 2 is sent to the aeration supply pipe 3, and this air is introduced into the aeration tank 12 from the fine holes or slits of the diffusion plate 4 through the inner tube 7. The operation is to discharge as fine bubbles. During the aeration operation, the on-off valve 18 is opened and the on-off valves 19, 20, 21 are closed for operation.

<水ブロー運転>
水ブロー運転とは、ブロー水供給手段5からブロー水を散気用給気配管3に定期的に供給し、内挿管7を介してブロー水を散気板4に供給することによって散気板4を水ブローし、散気板4の散気孔に微生物などが付着するのを防止する運転である。ブロー水の供給頻度に特に制限はないが、好ましくは数時間から数日毎にブロー水を散気用給気配管3内に供給する。
水ブロー運転においては、開閉弁18、21を開にし、開閉弁19、20を閉にして運転する。
<Water blow operation>
In the water blow operation, the blow water is periodically supplied from the blow water supply means 5 to the air supply pipe 3 for air diffusion, and the blow water is supplied to the air diffuser plate 4 via the inner intubation 7 to thereby diffuse the air diffuser plate. In this operation, water 4 is blown to prevent microorganisms and the like from adhering to the diffuser holes of the diffuser plate 4. There is no particular limitation on the supply frequency of the blow water, but preferably the blow water is supplied into the air supply pipe 3 for aeration every several hours to several days.
In the water blow operation, the on-off valves 18 and 21 are opened and the on-off valves 19 and 20 are closed.

<薬液による洗浄>
長期間に亘る散気運転を継続していると、ブロー水の定期的な供給を行なっていたとしても、散気板4にバイオフィルムが付着して散気板4での圧力損失が増大することがある。このような場合に行うのが薬液による洗浄であって、バイオフィルムなどを分解することができる薬液を用いて行うものである。
図6、図7は本実施の形態における薬液による洗浄方法の説明図である。以下、図1、図6、図7に基づいて薬液による洗浄方法を説明する。なお、図6、図7における開閉弁18、19、20、21については、弁が開状態のときには白抜きで表示し、弁が閉状態のときには黒塗りで表示している。
<Cleaning with chemicals>
If the aeration operation is continued for a long time, even if the blow water is regularly supplied, the biofilm adheres to the diffusion plate 4 and the pressure loss in the diffusion plate 4 increases. Sometimes. In such a case, cleaning with a chemical solution is performed using a chemical solution capable of decomposing a biofilm or the like.
6 and 7 are explanatory diagrams of a cleaning method using a chemical solution in the present embodiment. Hereinafter, a cleaning method using a chemical solution will be described with reference to FIG. 1, FIG. 6, and FIG. 6 and 7, the on-off valves 18, 19, 20, and 21 are displayed in white when the valve is open, and are displayed in black when the valve is closed.

散気運転を行なっている状態(図6(a)参照)から、薬液洗浄を行なう場合には、開閉弁18を閉止して散気用の給気を停止し、この状態で開閉弁19を開放して薬液注入装置14からアルカリ液を薬液注入管13を介して散気用給気配管3に所定量(例えば、ヘッダ管の半分の高さ程度)だけ注入する(図6(b)参照)。
なお、開閉弁18を閉止後は、散気用給気配管3内の圧力が散気板4に作用する水圧と同程度になるまで散気が継続され、前記水圧と散気用給気配管3内の圧力が同程度になると散気が行なわれなくなるが、このとき前記水圧と散気用給気配管3内の圧力がバランスしているので、汚水が散気板4から逆流することはない。
散気用給気配管3に注入されたアルカリ液は、図6(b)に示すように散気用給気配管3(ヘッダ)に貯留される。
In the case of performing chemical cleaning from the state where the aeration operation is performed (see FIG. 6A), the on-off valve 18 is closed to stop the air supply for the aeration, and the on-off valve 19 is turned on in this state. Opened and injects a predetermined amount (for example, about half the height of the header pipe) of the alkali liquid from the chemical liquid injection device 14 into the air supply pipe 3 for diffusion through the chemical liquid injection pipe 13 (see FIG. 6B). ).
After closing the on-off valve 18, the air diffusion is continued until the pressure in the air supply pipe 3 becomes the same as the water pressure acting on the air diffuser plate 4. However, since the water pressure and the pressure in the air supply pipe 3 are balanced at this time, the sewage does not flow backward from the air diffuser plate 4. Absent.
The alkaline liquid injected into the air supply piping 3 is stored in the air supply piping 3 (header) as shown in FIG. 6B.

次に、開閉弁19を閉止して薬液の注入を停止し、その後、開閉弁20を開放して空気注入管15を介して散気用給気配管3に加圧空気を所定時間(例えば、30分〜数時間程度)継続して少量づつ注入する(図6(c)参照)。加圧空気を散気用給気配管3に注入することにより、散気用給気配管3内の圧力が徐々に上昇し、図6(c)に示すように、アルカリ液が内挿管7に押し上げられ、散気板4にゆっくりと供給される。これによって、散気板4に付着したバイオフィルムがアルカリにより分解される。
なお、注入する加圧空気の量は、アルカリ液が散気板4にゆっくりと(じんわりと)供給されるような量にするのが望ましく、例えば散気板1枚当り0.01L/minとする。
Next, the on-off valve 19 is closed to stop the injection of the chemical solution, and then the on-off valve 20 is opened to supply pressurized air to the air supply pipe 3 for air diffusion through the air injection pipe 15 (for example, 30 minutes to several hours) Inject continuously in small portions (see FIG. 6C). By injecting the pressurized air into the air supply pipe 3 for air diffusion, the pressure in the air supply pipe 3 for air diffusion gradually rises, and as shown in FIG. It is pushed up and slowly supplied to the diffuser plate 4. Thereby, the biofilm adhering to the diffuser plate 4 is decomposed by alkali.
The amount of pressurized air to be injected is preferably such that the alkaline liquid is slowly (slowly) supplied to the diffuser plate 4, for example, 0.01 L / min per diffuser plate. To do.

加圧空気の注入を所定時間継続した後、開閉弁20を閉止し、開閉弁18を開放して散気用の空気を散気用給気配管3に供給する。さらに、開放弁21を開放してブロー水供給管17を介してブロー水を散気用給気配管3に供給する(図7(d)参照)。これによって、ブロー水が散気用の空気と共に散気板4に供給され、散気板4に残存しているバイオフィルムやアルカリ液をブローする。
その後、開閉弁21を閉止して、散気運転を継続する(図7(e)参照)。これによって、目詰まりが解消して目詰まりに起因する圧損が回復する。
After injecting the pressurized air for a predetermined time, the on-off valve 20 is closed, the on-off valve 18 is opened, and air for air diffusion is supplied to the air supply pipe 3 for air diffusion. Further, the release valve 21 is opened, and blow water is supplied to the air supply pipe 3 for aeration through the blow water supply pipe 17 (see FIG. 7D). Thereby, blow water is supplied to the diffuser plate 4 together with the air for aeration, and the biofilm and the alkaline liquid remaining on the diffuser plate 4 are blown.
Thereafter, the on-off valve 21 is closed and the aeration operation is continued (see FIG. 7E). As a result, clogging is eliminated and pressure loss due to clogging is recovered.

以上のように、本実施の形態の散気装置1は内挿管7を備えており、散気用給気管3(ヘッダ管)を水で満管にしなくてもブロー水を散気板4に供給することができるので、空気の供給通路は常に確保されている。従って、空気の供給中に定期的にブロー水を供給し、散気板4の散気孔に付着した微生物をブロー水で除去しながら、散気装置1を連続運転することができる。   As described above, the air diffuser 1 according to the present embodiment includes the inner tube 7, and blow water is supplied to the air diffuser plate 4 without filling the air diffuser air supply tube 3 (header tube) with water. Since the air can be supplied, the air supply passage is always secured. Accordingly, it is possible to continuously operate the air diffuser 1 while supplying blow water periodically during the air supply and removing the microorganisms adhering to the air diffuser holes of the air diffuser plate 4 with the blow water.

また、本実施の形態においては、散気用給気配管3に対する給気を停止した後、アルカリ液を散気用給気配管3内へ所定量供給し、その後散気用給気配管3内へ加圧空気を所定時間(例えば30分〜数時間)継続して供給するようにしたので、散気板4に対して所定時間(例えば30分〜数時間)継続してアルカリ液を供給でき、散気板4に付着したバイオフィルムを化学的に分解して、散気板4の目詰まりを効果的に回復することができる。
しかも、本実施の形態では、散気用給気管3(ヘッダ管)を満管にする必要がなく、アルカリ液は散気板4の洗浄に必要な量だけ供給すればよく、アルカリ液を無駄にすることがなく経済性に優れ、また曝気槽に多量のアルカリが混入することもないので、活性汚泥への悪影響の懸念も少ない。
Further, in the present embodiment, after the supply of air to the air supply pipe 3 for air diffusion is stopped, a predetermined amount of alkaline liquid is supplied into the air supply pipe 3 for air diffusion, and then the inside of the air supply pipe 3 for air diffusion Since the pressurized air is continuously supplied to the air diffuser for a predetermined time (for example, 30 minutes to several hours), the alkaline liquid can be continuously supplied to the diffuser plate 4 for a predetermined time (for example, 30 minutes to several hours). The clogging of the diffuser plate 4 can be effectively recovered by chemically decomposing the biofilm attached to the diffuser plate 4.
In addition, in the present embodiment, it is not necessary to fill the air supply pipe 3 (header pipe) for aeration, and it is only necessary to supply the alkali liquid in an amount necessary for cleaning the air diffuser plate 4 and waste the alkali liquid. Therefore, there is little concern about the adverse effect on activated sludge.

なお、上記の実施の形態においては、ブロー水について特に限定していないが、微生物を死滅させる効果を有する成分を含むブロー水を使用することによって、微生物の増殖を効果的に抑制することができる。微生物を死滅させる効果を有する成分には、特に制限はないが、例えば、抗菌物質または酸化物質、より具体的には、次亜塩素酸ナトリウム、逆性石鹸、酸、アルカリ、オゾン、または二酸化塩素、炭酸アルカリ金属などが含まれる。   In the above embodiment, the blow water is not particularly limited. However, the use of blow water containing a component having an effect of killing microorganisms can effectively suppress the growth of microorganisms. . The component having an effect of killing microorganisms is not particularly limited, but for example, an antibacterial substance or an oxidizing substance, more specifically, sodium hypochlorite, inverse soap, acid, alkali, ozone, or chlorine dioxide And alkali metal carbonates.

曝気槽12に、以下に示す仕様の散気板を設置し、下記の条件にて水ブローを実施し、水ブローの効果を確認した。   A diffuser plate having the following specifications was installed in the aeration tank 12, and water blowing was performed under the following conditions to confirm the effect of water blowing.

散気板材質:SUS316L
孔形状 :長さ1.45mm、幅0.04mm
開孔率 :約0.5%
通気量 :30m3/m2/hr
ブロー水 :次亜塩素酸ナトリウム溶液(濃度;100ppm)
ブロー水量:500ml/回
水ブロー頻度:1回/日
なお、水ブローを実施しない例を比較例とした。
Air diffuser material: SUS316L
Hole shape: Length 1.45mm, width 0.04mm
Opening ratio: about 0.5%
Air flow: 30m3 / m2 / hr
Blow water: Sodium hypochlorite solution (concentration: 100 ppm)
Blow water amount: 500 ml / time Water blow frequency: 1 time / day An example in which no water blow was performed was used as a comparative example.

水ブロー有りの例(実施例)となしの例(比較例)の圧損増加量(mmAq)の経時変化を、図8のグラフに示した。   The graph of FIG. 8 shows the change over time in the amount of increase in pressure loss (mmAq) in the example (Example) with and without water blow (Comparative Example).

図8のグラフから明らかなように、水ブローを定期的に実施することによって、長期間にわたる散気運転においても散気装置の圧損上昇を効果的に抑制することができ、高い酸素移動効率を維持することができた。   As is clear from the graph of FIG. 8, by periodically carrying out the water blow, it is possible to effectively suppress an increase in the pressure loss of the air diffuser even in the air diffused operation over a long period of time, and to achieve a high oxygen transfer efficiency. Could be maintained.

薬液洗浄の効果を確認するために以下のような3種類の実験を行なった。
<実験例1>
図9に示すように、24個の散気板4をヘッダ管22に設置した散気ブロックを曝気槽の水深1mの位置に配置し、1.5m/hr(散気板1枚当り)(30m3/m2/hr)で連続曝気した。
曝気開始時の散気板4の圧力損失は236mmAqであった。
曝気開始後300日経過したときの散気板4の圧力損失を測定したところ441mmAqであった。
そこで、以下に示す方法で薬液洗浄を行った。
ヘッダ管入り口の開閉弁23を閉じ、管内圧を水圧に対して正圧に保持しながら、薬液として5%NaOH溶液を全容積80Lのヘッダ管22に対し45L注水した。薬液注入後、エアポンプを用いてヘッダ管22内に空気を供給し、注入した薬液を空気で押出しながら内挿管7(図1参照)を介して散気板4に供給した。空気供給量は220ml/分とし、3時間継続して供給した。
空気による薬液押出しを終了した後、ろ過水をヘッダ管22内に48L供給し、開閉弁を開けてヘッダ管22内にブロア空気を導入して散気板4に水ブローを実施した。
水ブロー終了30分後に散気板4の圧力損失を測定したところ254mmAqであり、圧損の回復率は、91.2%であった。
このように、アルカリ液による薬液洗浄を実施することにより、散気板4の効果的な洗浄が実施できることが確認された。
In order to confirm the effect of chemical cleaning, the following three types of experiments were conducted.
<Experimental example 1>
As shown in FIG. 9, a diffuser block having 24 diffuser plates 4 installed on the header pipe 22 is arranged at a water depth of 1 m in the aeration tank, and 1.5 m 3 / hr (per diffuser plate) ( (30 m 3 / m 2 / hr) was continuously aerated.
The pressure loss of the diffuser plate 4 at the start of aeration was 236 mmAq.
It was 441 mmAq when the pressure loss of the diffuser plate 4 when 300 days passed after the start of aeration was measured.
Therefore, chemical cleaning was performed by the following method.
The on-off valve 23 at the inlet of the header pipe was closed, and 45 L of 5% NaOH solution was poured into the header pipe 22 having a total volume of 80 L as a chemical solution while maintaining the pipe internal pressure at a positive pressure relative to the water pressure. After injecting the chemical solution, air was supplied into the header pipe 22 using an air pump, and the injected chemical solution was supplied to the diffuser plate 4 through the inner tube 7 (see FIG. 1) while being extruded with air. The air supply rate was 220 ml / min, and the supply was continued for 3 hours.
After finishing the chemical solution extrusion by air, 48 L of filtered water was supplied into the header pipe 22, the on-off valve was opened, blower air was introduced into the header pipe 22, and water was blown into the diffuser plate 4.
When the pressure loss of the diffuser plate 4 was measured 30 minutes after the completion of the water blow, it was 254 mmAq, and the recovery rate of the pressure loss was 91.2%.
Thus, it was confirmed that effective cleaning of the diffuser plate 4 can be performed by performing chemical cleaning with an alkaline solution.

<実験例2>
実験例1と同じ条件で、薬液を5%NaOH+2%炭酸ナトリウムとした同様の実験例を行った。薬液洗浄後の圧力損失を測定したところ244mmAqであり、圧損の回復率は、96.1%であった。
このように、アルカリとして水酸化ナトリウムに炭酸ナトリウムを加えることでさらに洗浄効果が向上することが確認された。
<Experimental example 2>
Under the same conditions as in Experimental Example 1, a similar experimental example was performed in which the chemical solution was 5% NaOH + 2% sodium carbonate. The pressure loss after chemical cleaning was measured and found to be 244 mmAq. The recovery rate of pressure loss was 96.1%.
Thus, it was confirmed that the washing effect was further improved by adding sodium carbonate to sodium hydroxide as an alkali.

<実験例3>
実験例1のアルカリ薬液押出し終了後に、酸性薬剤として5%シュウ酸を45Lヘッダ管に注水し、実験例1と同様に空気による酸性薬液押出しを実施し、その後に実験例1と同様の水ブローを実施した。薬液洗浄後の圧力損失を測定したところ238mmAqであり、圧損の回復率は、99.0%であった。
このように、アルカリ洗浄後に酸による洗浄を行なうことで、アルカリ洗浄では洗浄できない例えば鉱物系の汚れを効果的に洗浄できることが確認された。
なお、実験例1〜3に示した圧力損失測定結果を以下の表1にまとめて示す。
<Experimental example 3>
After the completion of the extrusion of alkaline chemical solution in Experimental Example 1, 5% oxalic acid was injected into the 45 L header tube as an acidic chemical, and the acidic chemical solution was extruded with air in the same manner as in Experimental Example 1, and then the same water blow as in Experimental Example 1 was performed. Carried out. The pressure loss after chemical cleaning was measured and found to be 238 mmAq. The recovery rate of pressure loss was 99.0%.
As described above, it was confirmed that, for example, mineral-based soil that cannot be cleaned by alkali cleaning can be effectively cleaned by performing cleaning with acid after alkali cleaning.
The pressure loss measurement results shown in Experimental Examples 1 to 3 are summarized in Table 1 below.

Figure 0005062138
Figure 0005062138

本発明の一実施の形態に係る散気装置の模式図である。It is a mimetic diagram of an air diffuser concerning one embodiment of the present invention. 本発明の一実施の形態に係る内挿管の断面図である。It is sectional drawing of the intubation which concerns on one embodiment of this invention. 本発明の一実施の形態に係る内挿管の一態様を示す図であり、吸込み面が傾斜していない場合の模式図である。It is a figure which shows the one aspect | mode of the intubation tube which concerns on one embodiment of this invention, and is a schematic diagram in case the suction surface is not inclined. 本発明の一実施の形態に係る内挿管の他の態様を示す図であり、吸込み面が傾斜している場合の模式図である。It is a figure which shows the other aspect of the intubation tube which concerns on one embodiment of this invention, and is a schematic diagram in case the suction surface inclines. 本発明の一実施の形態における内挿管の作用の説明図である。It is explanatory drawing of the effect | action of the intubation in one embodiment of this invention. 本発明の一実施の形態における薬液による洗浄方法の説明図である。It is explanatory drawing of the washing | cleaning method by the chemical | medical solution in one embodiment of this invention. 本発明の一実施の形態における薬液による洗浄方法の説明図である。It is explanatory drawing of the washing | cleaning method by the chemical | medical solution in one embodiment of this invention. 実施例1の圧損増加量の経時変化を示すグラフである。3 is a graph showing the change over time in the amount of increase in pressure loss in Example 1. 実施例2の実験例の説明図である。6 is an explanatory diagram of an experimental example of Example 2. FIG.

符号の説明Explanation of symbols

1 散気装置
2 ガス供給手段
3 散気用給気配管
4 散気板
5 ブロー水供給手段
7 内挿管
8 吸い込み面
9 通気孔
10 固定用締付け部材
11 取付ブラケット
12 曝気槽
13 薬液注入管
14 薬液注入装置
15 空気注入管
16 加圧空気供給装置
17 ブロー水供給管
18、19、20、21、23 開閉弁
22 ヘッダ管
θ 傾斜角度
DESCRIPTION OF SYMBOLS 1 Air diffuser 2 Gas supply means 3 Air supply piping for aeration 4 Air diffuser plate 5 Blow water supply means 7 Inner intubation 8 Suction surface 9 Vent 10 Fixing member 11 Mounting bracket 12 Aeration tank 13 Chemical solution injection pipe 14 Chemical solution Injection device 15 Air injection pipe 16 Pressurized air supply device 17 Blow water supply pipe 18, 19, 20, 21, 23 On-off valve 22 Header pipe θ Inclination angle

Claims (4)

曝気槽に設置される微細気孔を有する散気板と、該散気板に接続された散気用給気配管と、該散気用給気配管に開閉弁を介して接続されて該散気用給気配管に散気用空気を供給する給気装置と、一端が前記散気板に連接され、他端が前記散気用給気配管内に内挿された内挿管とを備えた散気装置の洗浄方法であって、
前記散気用給気配管に加圧空気を注入する加圧空気供給装置と、前記散気用給気配管に洗浄薬液を注入する薬液注入装置とを設け、
前記開閉弁を閉止して散気用給気配管に対する前記散気用空気の給気を停止した後、前記薬液注入装置によって洗浄液を前記散気用給気配管内へ供給する洗浄液供給工程と、前記加圧空気供給装置によって前記散気用給気配管内へ加圧空気を30分〜数時間継続して供給し、前記散気用給気配管内の洗浄液を前記内挿管を介して散気板から継続して排出させる散気板薬液洗浄工程を備えたことを特徴とする散気装置の洗浄方法。
A diffuser plate having fine pores installed in the aeration tank, a diffuser air supply pipe connected to the diffuser plate, and the diffuser connected to the diffuser air supply pipe via an open / close valve An air supply comprising an air supply device for supplying air for diffusion to an air supply pipe, and an intubation pipe having one end connected to the air diffuser plate and the other end inserted into the air supply pipe for air diffusion A method for cleaning an apparatus,
A pressurized air supply device for injecting pressurized air into the air supply pipe for air diffusion, and a chemical liquid injection device for injecting a cleaning chemical into the air supply pipe for air diffusion,
After stopping the supply of the air diffuser for air to air air supply piping scattered by closing the on-off valve, the cleaning agent liquid supply for supplying a cleaning agent liquid feeding to sign tube for the air diffuser by the liquid injector a step, and continuously supplied to the pressurized air supply device by said air diffuser for supply to the sign tube pressurized air 30 minutes to several hours, through the intubation cleaning agent liquid of the air diffuser for supply quotations tube A method for cleaning an air diffuser comprising a chemical cleaning process for an air diffuser that continuously discharges from an air diffuser.
散気用給気配管内にブロー水を供給するブロー水供給手段を設け、洗浄液による洗浄後、前記ブロー水供給手段によって散気用給気配管内にブロー水を供給すると共に散気用給気配管内に散気用空気を送風して該ブロー水を内挿管を介して散気板に供給して水ブローする水ブロー工程を備えたことを特徴とする請求項1に記載の散気装置の洗浄方法。 Provided blow water supply means for supplying blow water supply quotations tube for aeration, after washing with the washing agent solution, air diffuser for feeding signs supplies blow water supply quotations tube for air diffuser by said blowing water supplier The air diffuser according to claim 1, further comprising a water blowing step for blowing air into the pipe and supplying the blow water to the diffuser plate through an intubation tube to blow the water. Cleaning method. 洗浄液が、アルカリを主成分とした薬液であることを特徴とする請求項1または2に記載の散気装置の洗浄方法。 Irrigant fluid, the cleaning method of the air diffuser device according to claim 1 or 2, characterized in that a chemical solution composed mainly of an alkali. 洗浄液が、炭酸ナトリウムを含有することを特徴とする請求項3に記載の散気装置の洗浄方法。
Method of cleaning an air diffuser apparatus according to claim 3, irrigant fluid, characterized in that it contains sodium carbonate.
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