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JP6918667B2 - Cleaning method of air diffuser and air diffuser - Google Patents
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JP6918667B2 - Cleaning method of air diffuser and air diffuser - Google Patents

Cleaning method of air diffuser and air diffuser Download PDF

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JP6918667B2
JP6918667B2 JP2017189435A JP2017189435A JP6918667B2 JP 6918667 B2 JP6918667 B2 JP 6918667B2 JP 2017189435 A JP2017189435 A JP 2017189435A JP 2017189435 A JP2017189435 A JP 2017189435A JP 6918667 B2 JP6918667 B2 JP 6918667B2
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pipe
air
air diffuser
diffuser
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JP2019063707A (en
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矢ノ根 勝行
勝行 矢ノ根
信也 末吉
信也 末吉
哲也 大城
哲也 大城
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Mitsubishi Chemical Aqua Solutions Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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Description

本発明は、散気装置の洗浄方法及び散気装置に関するものである。 The present invention relates to a method for cleaning an air diffuser and an air diffuser.

近年、工業排水や生活排水等の排水の処理として、活性汚泥を含む被処理液が充填された水槽と、該水槽内に配置された膜モジュールと、膜モジュールの下方に配置された散気管を備えた水処理装置を用いた膜分離活性汚泥法(MBR)による処理が種々検討されている。MBRによる処理では、前記被処理液が前記膜モジュールにより固液分離され水質の高い処理水が得られる。 In recent years, as a treatment of wastewater such as industrial wastewater and domestic wastewater, a water tank filled with a liquid to be treated containing activated sludge, a membrane module arranged in the water tank, and an air diffuser pipe arranged below the membrane module have been provided. Various treatments by the membrane separation activated sludge method (MBR) using the provided water treatment apparatus have been studied. In the treatment by MBR, the liquid to be treated is solid-liquid separated by the membrane module to obtain treated water having high water quality.

MBRにおいて、膜モジュールにより被処理液の固液分離を継続して行うと、膜モジュールに配設された分離膜の表面が懸濁物質により目詰まりし、膜モジュールの膜間差圧が上昇し、膜モジュールによる固液分離で得られる単位時間当たりの処理水量が低下する。そこで、MBRにおいては、膜モジュールの下方に配置された散気管から気体を散気することによって気泡を生じさせ、該気泡の上昇によって形成される気泡と被処理液との気液混合流を分離膜の表面に接触させることにより、分離膜の表面に付着した汚泥等の懸濁物質を除去する洗浄を行いながら固液分離が行われている。 In MBR, when the solid-liquid separation of the liquid to be treated is continuously performed by the membrane module, the surface of the separation membrane disposed on the membrane module is clogged with the suspended substance, and the intermembrane differential pressure of the membrane module increases. , The amount of treated water per unit time obtained by solid-liquid separation by the membrane module decreases. Therefore, in the MBR, bubbles are generated by aerating gas from an aeration tube arranged below the membrane module, and the gas-liquid mixed flow of the bubbles formed by the rise of the bubbles and the liquid to be treated is separated. Solid-liquid separation is performed while cleaning to remove suspended substances such as sludge adhering to the surface of the separation membrane by bringing it into contact with the surface of the membrane.

このようなMBRにおいては、処理が継続されるにしたがって、水槽内の汚泥が散気管内に徐々に入り込んで乾燥し堆積物を生じることがあった。この堆積物は散気管を閉塞して散気を不安定にする原因となる。散気管からの散気が不安定になると、分離膜の表面に対して気泡を含む気液混合流を充分に接触させることが困難となり、分離膜の表面に付着した懸濁物質が充分に除去されなくなる。これにより膜モジュールの膜間差圧が上昇し、膜モジュールによる固液分離で得られる単位時間当たりの処理水量が低下する。
かかる問題に対して、従来、水槽内から散気管を引き上げて、散気管に堆積した堆積物を除去する洗浄が行われていた。しかし、散気管を引き上げて洗浄する洗浄方法は、時間がかかり洗浄コストも高くなる。特に、散気管と膜モジュールが一体化された装置の散気管を洗浄する場合には、該装置自体を水槽内から引き上げる必要があり、散気管の洗浄に要する時間及び洗浄コストが多大となる。
In such an MBR, as the treatment was continued, sludge in the water tank may gradually enter the air diffuser pipe and dry out to form deposits. This deposit causes obstruction of the air diffuser and destabilization of air diffuser. When the air diffused from the air diffuser becomes unstable, it becomes difficult to sufficiently bring the gas-liquid mixed flow containing air bubbles into contact with the surface of the separation membrane, and the suspended solids adhering to the surface of the separation membrane are sufficiently removed. Will not be. As a result, the differential pressure between the membranes of the membrane module increases, and the amount of treated water per unit time obtained by solid-liquid separation by the membrane module decreases.
In response to this problem, conventionally, cleaning has been performed by pulling up the air diffuser pipe from the inside of the water tank to remove the deposits accumulated on the air diffuser pipe. However, the cleaning method in which the air diffuser is pulled up for cleaning is time-consuming and increases the cleaning cost. In particular, when cleaning the air diffuser of a device in which the air diffuser and the membrane module are integrated, it is necessary to pull the device itself out of the water tank, which increases the time and cleaning cost required for cleaning the air diffuser.

特許文献1には、槽内に浸漬した散気管に基端側から空気を供給し、散気管の下方に設けた複数の空気噴出口から空気を散気する散気装置において、散気管に空気を供給する状態で散気管の先端側に接続した散気ドレン管のドレンバルブを開放し、散気管に供給する空気を散気ドレン管を通して排気し、空気噴出口から散気管内に槽内液を逆流入させて散気管を水洗浄し、散気管内の圧力変化に由来して生じる脈動を利用して断続的に水洗浄を繰り返す技術が開示されている。 Patent Document 1 describes in an air diffuser that supplies air to an air diffuser immersed in a tank from the proximal end side and dissipates air from a plurality of air outlets provided below the air diffuser. The drain valve of the air diffuser drain pipe connected to the tip side of the air diffuser pipe is opened, the air supplied to the air diffuser pipe is exhausted through the air diffuser drain pipe, and the liquid in the tank is discharged from the air outlet into the air diffuser pipe. Disclosed is a technique in which the air diffuser is washed with water by reverse inflowing the air, and the water is washed intermittently by utilizing the pulsation generated by the pressure change in the air diffuser.

特許第3382926号公報Japanese Patent No. 3382926

しかしながら、特許文献1に記載された技術では、散気管のうち空気供給側である基端側は先端側と比較して槽内の液体が流入しづらいため、供給された空気による散気管内の液体の乾燥が進み散気穴の閉塞を生じさせる可能性がある。また、特許文献1に記載された散気装置は、散気管の基端側に空気供給管を配置し、散気管の先端側に散気ドレン管及びドレンバルブを配置しているため、散気ドレン管及びドレンバルブを設置するためのスペースを別途確保する必要が生じ装置の大型化を招いてしまう。 However, in the technique described in Patent Document 1, the liquid in the tank is less likely to flow into the base end side of the air diffuser pipe, which is the air supply side, as compared with the tip side. Drying of the liquid may progress and cause blockage of the air diffuser holes. Further, in the air diffuser described in Patent Document 1, an air supply pipe is arranged on the base end side of the air diffuser pipe, and an air diffuser drain pipe and a drain valve are arranged on the tip end side of the air diffuser pipe. It is necessary to separately secure a space for installing the drain pipe and the drain valve, which leads to an increase in the size of the device.

本発明は、以上のような点を考慮してなされたもので、装置の大型化を招くことなく散気管の目詰まりおよび閉塞を抑制できる散気装置の洗浄方法及び散気装置を提供することを目的とする。 The present invention has been made in consideration of the above points, and provides a method for cleaning an air diffuser and an air diffuser capable of suppressing clogging and blockage of an air diffuser without causing an increase in size of the device. With the goal.

本発明は以下の態様を有する。
[1]水槽内に浸漬した散気管に給気管から空気を供給し、前記散気管の空気噴出口から空気を散気する散気工程が行われる散気装置の洗浄方法であって、
大気開放弁が設けられ前記散気管の一端側に接続した前記給気管と、
開閉弁が設けられ前記散気管の一端側に接続した排出管とを準備する工程と、
前記開閉弁を閉塞するとともに前記給気管からの空気の供給を停止した状態で、前記大気開放弁を開放して前記散気管の内部を大気開放し、前記空気噴出口を介して前記水槽内の液体を前記散気管の内部に充満させる充満工程と、
前記大気開放弁を閉塞するとともに前記開閉弁を開放した状態で、前記給気管から空気を供給して前記散気管の一端側を介して前記排出管に送出することにより、前記空気噴出口を介して前記給気管の内部に流入した液体を前記排出管を介して排出する排出工程と、
を含む。
[2]前記充満工程の後に前記散気工程を行う第1モードと、前記充満工程の後に前記排出工程及び前記散気工程を順次行う第2モードとを含む前記[1]記載の散気装置の洗浄方法。
[3]前記第1モードは、前記大気開放弁の開放時間が一回あたり10秒以上であり、一日一回以上、24回以下行われる前記[2]記載の散気装置の洗浄方法。
[4]前記第2モードは、前記開閉弁の開放時間が10秒以上であり、二週間に一回以上、一日一回以下行われる前記[2]または前記[3]記載の散気装置の洗浄方法。
[5]前記排出管の管径は、給気管の管径の1.1倍以上、2倍以下である前記[1]から前記[4]のいずれか一項に記載の散気装置の洗浄方法。
[6]前記散気装置は、鉛直方向に延び間隔をあけて配置された第1配管及び第2配管と、前記第1配管及び前記第2配管の下端同士を接続し前記散気管の一端側が中途に接続された第3配管とを有し、前記第1配管と、前記第3配管の前記散気管との接続部よりも長さ方向の一方側とは、前記給気管を形成し、前記第2配管と、前記第3配管の前記散気管との接続部よりも長さ方向の他方側とは、前記排気管を形成する前記[1]から前記[5]のいずれか一項に記載の散気装置の洗浄方法。
[7]水槽内に浸漬され空気噴出口を有する散気管を備えた散気装置であって、大気開放弁が設けられ前記散気管の一端側に接続され前記散気管に空気を供給可能な給気管と、開閉弁が設けられ前記散気管の一端側に接続され前記散気管の内部に流入した液体を排出可能な排出管とを備える散気装置。
[8]鉛直方向に延び間隔をあけて配置された第1配管及び第2配管と、前記第1配管及び前記第2配管の下端同士を接続し前記散気管の一端側が中途に接続された第3配管とを有し、前記第1配管と、前記第3配管の前記散気管との接続部よりも長さ方向の一方側とは、前記給気管を形成し、前記第2配管と、前記第3配管の前記散気管との接続部よりも長さ方向の他方側とは、前記排気管を形成する前記[7]記載の散気装置。
[9]前記開閉弁を閉塞するとともに前記給気管からの空気の供給を停止した状態で、前記大気開放弁を開放して前記散気管の内部を大気開放し、前記空気噴出口を介して前記水槽内の液体を前記散気管の内部に充満させた後に、前記大気開放弁を閉塞するとともに前記開閉弁を開放した状態で、前記給気管から空気を供給させ前記散気管の一端側を介して前記排出管に送出することにより、前記空気噴出口を介して前記給気管の内部に流入した液体を前記排出管を介して排出させる制御部を有する前記[7]または前記[8]に記載の散気装置。
[10]前記制御部は、前記散気管の内部を大気開放し、前記水槽内の液体を前記散気管の内部に充満させた後に、前記散気管に前記給気管から空気を供給させ前記空気噴出口から空気を散気させる第1モードと、前記散気管の内部を大気開放し、前記水槽内の液体を前記散気管の内部に充満させた後に、前記給気管から空気を供給させ前記散気管の一端側を介して前記排出管に送出することにより、前記空気噴出口を介して前記給気管の内部に流入した液体を前記排出管を介して排出させ、その後に前記散気管に前記給気管から空気を供給させ前記空気噴出口から空気を散気させる第2モードとを有する前記[9]記載の散気装置。
The present invention has the following aspects.
[1] A method for cleaning an air diffuser, in which an air diffuser step of supplying air from an air supply pipe to an air diffuser immersed in a water tank and airing air from an air outlet of the air diffuser is performed.
The air supply pipe provided with an air release valve and connected to one end side of the air diffuser pipe,
A step of preparing a discharge pipe provided with an on-off valve and connected to one end side of the air diffuser pipe, and
With the on-off valve closed and the air supply from the air supply pipe stopped, the air release valve is opened to open the inside of the air diffuser pipe to the atmosphere, and the inside of the water tank is opened via the air outlet. The filling process of filling the inside of the air diffuser with liquid,
With the air release valve closed and the on-off valve open, air is supplied from the air supply pipe and sent out to the discharge pipe via one end side of the air diffuser pipe, thereby passing through the air outlet. And the discharge process of discharging the liquid that has flowed into the inside of the air supply pipe through the discharge pipe.
including.
[2] The air diffuser according to the above [1], which includes a first mode in which the air dissipating step is performed after the filling step, and a second mode in which the discharging step and the air dissipating step are sequentially performed after the filling step. Cleaning method.
[3] The method for cleaning an air diffuser according to the above [2], wherein the first mode is performed once a day or more and 24 times or less, with the opening time of the atmospheric release valve being 10 seconds or more each time.
[4] The air diffuser according to the above [2] or [3], wherein in the second mode, the opening time of the on-off valve is 10 seconds or more, and the opening time is performed once every two weeks or more and once a day or less. Cleaning method.
[5] Cleaning of the air diffuser according to any one of [1] to [4], wherein the diameter of the discharge pipe is 1.1 times or more and 2 times or less the diameter of the air supply pipe. Method.
[6] In the air diffuser, the first pipe and the second pipe arranged at intervals extending in the vertical direction and the lower ends of the first pipe and the second pipe are connected to each other, and one end side of the air diffuser is connected. The air supply pipe is formed by having a third pipe connected in the middle, and one side of the first pipe and one side of the third pipe in the length direction with respect to the connection portion of the air diffuser pipe. The other side of the second pipe and the other side of the third pipe in the length direction from the connection portion with the air diffuser pipe is described in any one of the above [1] to the above [5] forming the exhaust pipe. How to clean the air diffuser.
[7] An air diffuser having an air diffuser immersed in a water tank and having an air outlet, which is provided with an air release valve and is connected to one end side of the air diffuser to supply air to the air diffuser. An air diffuser including a trachea and an air diffuser provided with an on-off valve and connected to one end side of the air diffuser so as to be able to discharge the liquid flowing into the air diffuser.
[8] A first pipe and a second pipe that extend in the vertical direction and are arranged at intervals, and the lower ends of the first pipe and the second pipe are connected to each other, and one end side of the air diffuser pipe is connected halfway. The first pipe and one side of the third pipe in the length direction with respect to the connection portion of the third pipe form the air supply pipe, and the second pipe and the second pipe and the air supply pipe are formed. The air diffuser according to the above [7], wherein the other side of the third pipe in the length direction from the connection portion with the air diffuser is the exhaust pipe.
[9] With the on-off valve closed and the air supply from the air supply pipe stopped, the air release valve is opened to open the inside of the air diffuser pipe to the atmosphere, and the air outlet is used to open the inside of the air diffuser. After filling the inside of the air diffuser with the liquid in the water tank, air is supplied from the air supply pipe in a state where the air release valve is closed and the on-off valve is open, and air is supplied from the air supply pipe through one end side of the air diffuser. The above [7] or the above [8], which has a control unit for discharging the liquid that has flowed into the inside of the air supply pipe through the air outlet by sending it to the discharge pipe. Air diffuser.
[10] The control unit opens the inside of the air diffuser pipe to the atmosphere, fills the inside of the air diffuser pipe with the liquid in the water tank, and then supplies air to the air diffuser pipe from the air supply pipe to inject the air. In the first mode in which air is dissipated from the outlet, the inside of the air diffuser is opened to the atmosphere, the liquid in the water tank is filled in the air diffuser, and then air is supplied from the air supply pipe to the air diffuser. The liquid that has flowed into the air supply pipe through the air outlet is discharged through the discharge pipe by delivering the liquid to the discharge pipe via one end side of the air outlet, and then the air supply pipe is discharged to the air diffuser. The air diffuser according to the above [9], which has a second mode in which air is supplied from the air outlet and air is diffused from the air outlet.

本発明では、装置の大型化を招くことなく散気管の目詰まりおよび閉塞を抑制することが可能になる。 According to the present invention, it is possible to suppress clogging and blockage of the air diffuser pipe without causing an increase in size of the device.

本発明の一実施形態の散気装置30を備える水処理装置1の概略構成図である。It is a schematic block diagram of the water treatment apparatus 1 provided with the air diffuser 30 of one Embodiment of this invention. 散気管13、給気管31及び排出管41の一部を示す正面図である。It is a front view which shows a part of an air diffuser pipe 13, an air supply pipe 31 and a discharge pipe 41. 図2の右側面図である。It is a right side view of FIG. 散気装置30の制御に係るブロック図である。It is a block diagram which concerns on the control of the air diffuser 30.

以下、本発明の散気装置の洗浄方法及び散気装置の実施の形態を、図1ないし図4を参照して説明する。
なお、以下の実施形態は、本発明の一態様を示すものであり、この発明を限定するものではなく、本発明の技術的思想の範囲内で任意に変更可能である。また、以下の図面においては、各構成をわかりやすくするために、実際の構造と各構造における縮尺や数等を異ならせている。
Hereinafter, a method for cleaning the air diffuser and an embodiment of the air diffuser of the present invention will be described with reference to FIGS. 1 to 4.
It should be noted that the following embodiments show one aspect of the present invention, do not limit the present invention, and can be arbitrarily changed within the scope of the technical idea of the present invention. Further, in the following drawings, in order to make each configuration easy to understand, the scale and number of each structure are different from the actual structure.

図1は、本発明の一実施形態の散気装置30を備える水処理装置1の概略構成図である。
水処理装置1は、膜分離活性汚泥法による水処理装置である。
この実施形態の水処理装置1は、水槽11と、水槽11内に配置された膜モジュール12と、膜モジュール12で分離された処理水を排出する処理水排出管15と、膜モジュール11の下方から気泡を散気させる散気装置30と、制御部CONT(図4参照)を備えている。
FIG. 1 is a schematic configuration diagram of a water treatment device 1 including an air diffuser 30 according to an embodiment of the present invention.
The water treatment device 1 is a water treatment device by the membrane separation activated sludge method.
The water treatment device 1 of this embodiment includes a water tank 11, a membrane module 12 arranged in the water tank 11, a treated water discharge pipe 15 for discharging the treated water separated by the membrane module 12, and a lower portion of the membrane module 11. It is provided with an air diffuser 30 for dissipating air bubbles from the air, and a control unit CONT (see FIG. 4).

<水槽11>
水槽11は、一例として、活性汚泥の作用により工業排水等の被処理液が生物処理されて生物処理水とされる槽である。水槽11は、特に限定されないが、例えば直方体状のもので、深さは、被処理液の水深が1m以上となるように、1mを超えることが好ましい。
水槽11には、排水が貯留された原水槽(図示せず)からの排水が供給される排水供給管(図示せず)が接続されている。
水槽11内には、膜モジュール12が配置されている。水槽11内には、活性汚泥を含む被処理液が充填され、散気装置30で生じる散気により活性汚泥処理(生物処理)が行われる。生物処理された処理水は、膜モジュール12により固液分離される。
<Aquarium 11>
As an example, the water tank 11 is a tank in which a liquid to be treated such as industrial wastewater is biologically treated by the action of activated sludge to be treated as biologically treated water. The water tank 11 is not particularly limited, but is, for example, a rectangular parallelepiped, and the depth is preferably more than 1 m so that the water depth of the liquid to be treated is 1 m or more.
A drainage supply pipe (not shown) for supplying drainage from a raw water tank (not shown) in which drainage is stored is connected to the water tank 11.
The membrane module 12 is arranged in the water tank 11. The water tank 11 is filled with a liquid to be treated containing activated sludge, and activated sludge treatment (biological treatment) is performed by the dust generated by the air diffuser 30. The biologically treated treated water is solid-liquid separated by the membrane module 12.

<膜モジュール12>
膜モジュール12は、水槽11内に配置される。膜モジュール12には、処理水排出管15が接続されている。
処理水排出管15には、その流路の途中に吸引ポンプ17が設けられている。吸引ポンプ17により、膜モジュール12内が減圧され活性汚泥と処理水(透過水)とが固液分離される。さらに処理水が、処理水排出管15を経て水槽11の外側に排出される。
<Membrane module 12>
The membrane module 12 is arranged in the water tank 11. A treated water discharge pipe 15 is connected to the membrane module 12.
The treated water discharge pipe 15 is provided with a suction pump 17 in the middle of the flow path thereof. The suction pump 17 depressurizes the inside of the membrane module 12 and separates the activated sludge and the treated water (permeated water) into solid and liquid. Further, the treated water is discharged to the outside of the water tank 11 through the treated water discharge pipe 15.

膜モジュール12としては、公知の分離膜(ろ過膜)を備えた公知の膜モジュールを用いることができる。
分離膜の種類としては、精密ろ過膜(MF膜)又は限外ろ過膜(UF膜)が好ましい。
分離膜の形状としては、中空糸膜、平膜、管状膜、袋状膜等が挙げられる。これらのうち、容積ベースで比較した場合に膜面積の高度集積が可能であることから、中空糸膜が好ましい。
As the membrane module 12, a known membrane module provided with a known separation membrane (filtration membrane) can be used.
As the type of separation membrane, a microfiltration membrane (MF membrane) or an ultrafiltration membrane (UF membrane) is preferable.
Examples of the shape of the separation membrane include a hollow fiber membrane, a flat membrane, a tubular membrane, and a bag-shaped membrane. Of these, the hollow fiber membrane is preferable because the membrane area can be highly integrated when compared on a volume basis.

分離膜の材質としては、有機材料(セルロース、ポリオレフィン、ポリスルフォン、ポリビニルアルコール、ポリメチルメタクリレート、ポリフッ化ビニリデン、ポリ4フッ化エチレン等)、金属(ステンレス等)、無機材料(セラミック等)が挙げられる。分離膜の材質は、排水の性状等に応じて適宜選択される。 Examples of the material of the separation membrane include organic materials (cellulose, polyolefin, polysulfone, polyvinyl alcohol, polymethylmethacrylate, polyvinylidene fluoride, polytetrafluoroethylene, etc.), metals (stainless steel, etc.), and inorganic materials (ceramic, etc.). Be done. The material of the separation membrane is appropriately selected according to the properties of drainage and the like.

分離膜の孔径は、処理の目的に応じて適宜選択すればよい。MBRにおいて、分離膜の孔径は、0.001〜3μmが好ましい。孔径が0.001μm未満では、膜の抵抗が大きくなりやすい。孔径が3μmを超えると、汚泥を完全に分離することができないため、処理水(透過水)の水質が悪化するおそれがある。分離膜の孔径は、精密ろ過膜の範囲とされる0.04〜1.0μmがより好ましい。
膜モジュール12は、水槽内11内に1つ配備されてもよいし複数配備されてもよい。
The pore size of the separation membrane may be appropriately selected according to the purpose of the treatment. In the MBR, the pore size of the separation membrane is preferably 0.001 to 3 μm. If the pore size is less than 0.001 μm, the resistance of the film tends to increase. If the pore size exceeds 3 μm, sludge cannot be completely separated, so that the quality of treated water (permeated water) may deteriorate. The pore size of the separation membrane is more preferably 0.04 to 1.0 μm, which is in the range of the microfiltration membrane.
One membrane module 12 may be deployed in the water tank 11, or a plurality of membrane modules 12 may be deployed.

<散気装置30>
散気装置30は、散気管13と、散気管13の一端側(図1では右側)に接続された給気管31と、散気管13の一端側に接続された排出管41とを有している。
<Air diffuser 30>
The air diffuser 30 has an air diffuser 13, an air supply pipe 31 connected to one end side (right side in FIG. 1) of the air diffuser 13, and a discharge pipe 41 connected to one end side of the air diffuser 13. There is.

散気管13としては、特に限定されない。図2及び図3に散気管13の一例を示す。
図2は、散気管13、給気管31及び排出管41の一部を示す正面図である。図3は、図2の右側面図である。
The air diffuser 13 is not particularly limited. 2 and 3 show an example of the air diffuser 13.
FIG. 2 is a front view showing a part of the air diffuser pipe 13, the air supply pipe 31, and the discharge pipe 41. FIG. 3 is a right side view of FIG.

図2及び図3に示すように、散気管13は、給気管31を介して気体が供給される水平方向に延びる主配管2と、主配管2に直接連結して水平方向に延びる複数の枝配管3と、を備える。主配管2は、後述するように、長さ方向の一端側において給気管31及び排出管41に接続されている。主配管2の他端側は、開口することなく、蓋2aが被着されていることによって気密に閉塞されている。 As shown in FIGS. 2 and 3, the air diffuser pipe 13 includes a main pipe 2 extending in the horizontal direction in which gas is supplied via the air supply pipe 31, and a plurality of branches extending in the horizontal direction directly connected to the main pipe 2. It is provided with a pipe 3. As will be described later, the main pipe 2 is connected to the air supply pipe 31 and the discharge pipe 41 on one end side in the length direction. The other end side of the main pipe 2 is hermetically closed by being covered with the lid 2a without opening.

主配管2は、水平に配された状態で、その下部から下方に向かって延びる鉛直管部6が、主配管2内に連通して設けられている。鉛直管部6の下端側には、T字状に形成された三方管7が設けられている。三方管7の両側には、それぞれ枝配管3の一端側が接続されている。枝配管3は、主配管2と直交する方向に延びて配置されている。枝配管3の下側には、空気噴出口8が1つ以上形成されている。また、枝配管3は、その他端の近傍に屈曲部3aが形成されていることにより、主配管2を水平に配した状態で、他端の開口3bが鉛直方向下方に向くよう構成されている。 The main pipe 2 is arranged horizontally, and a vertical pipe portion 6 extending downward from the lower portion thereof is provided so as to communicate with the inside of the main pipe 2. A T-shaped three-way pipe 7 is provided on the lower end side of the vertical pipe portion 6. One end side of the branch pipe 3 is connected to both sides of the three-way pipe 7. The branch pipe 3 is arranged so as to extend in a direction orthogonal to the main pipe 2. One or more air outlets 8 are formed on the lower side of the branch pipe 3. Further, the branch pipe 3 is configured such that the opening 3b at the other end faces downward in the vertical direction while the main pipe 2 is arranged horizontally because the bent portion 3a is formed near the other end. ..

図1に戻り、給気管31には、その流路の途中にブロワ32が設けられている。また、給気管31における散気管13とブロワ32との間には、大気開放弁33が設けられている。給気管31は、大気開放弁33が開放されたときに大気開放され、大気開放弁33が閉塞したときに大気開放が解除される。 Returning to FIG. 1, the air supply pipe 31 is provided with a blower 32 in the middle of the flow path thereof. Further, an air release valve 33 is provided between the air diffuser pipe 13 and the blower 32 in the air supply pipe 31. The air supply pipe 31 is opened to the atmosphere when the air release valve 33 is opened, and is released to the atmosphere when the air release valve 33 is closed.

排出管41は、散気管13の内部に流入した液体を排出可能である。排出管41には、その流路の途中に開閉弁42が設けられている。排出管41から排出された液体は、水槽11内に戻される。 The discharge pipe 41 can discharge the liquid that has flowed into the inside of the air diffuser pipe 13. The discharge pipe 41 is provided with an on-off valve 42 in the middle of the flow path thereof. The liquid discharged from the discharge pipe 41 is returned to the water tank 11.

図3に示すように、給気管31は、鉛直方向に延びる第1配管51と、第1配管51の下端に接続された第3配管53の一部とを含む。排出管41は、鉛直方向に延びる第2配管52と、第2配管52の下端に接続された第3配管53の一部とを含む。第1配管51及び第2配管52は、散気管13の一端側において主配管2と直交する方向に間隔をあけて配置されている。第3配管53は、第1配管51及び第2配管52の下端同士を接続している。第3配管53は、主配管2と同じ高さに配置されており、主配管2の一端側が中途において接続されている。従って、第1配管51と、第3配管53の主配管2との接続部よりも第1配管51側とは、給気管31を形成している。また、第2配管52と、第3配管53の主配管2との接続部よりも第2配管52側とは、排出管41を形成している。 As shown in FIG. 3, the air supply pipe 31 includes a first pipe 51 extending in the vertical direction and a part of a third pipe 53 connected to the lower end of the first pipe 51. The discharge pipe 41 includes a second pipe 52 extending in the vertical direction and a part of the third pipe 53 connected to the lower end of the second pipe 52. The first pipe 51 and the second pipe 52 are arranged at one end side of the air diffuser pipe 13 at intervals in a direction orthogonal to the main pipe 2. The third pipe 53 connects the lower ends of the first pipe 51 and the second pipe 52 to each other. The third pipe 53 is arranged at the same height as the main pipe 2, and one end side of the main pipe 2 is connected in the middle. Therefore, the air supply pipe 31 is formed between the first pipe 51 and the first pipe 51 side of the connection portion between the main pipe 2 of the third pipe 53. Further, a discharge pipe 41 is formed between the second pipe 52 and the second pipe 52 side of the connection portion between the second pipe 52 and the main pipe 2 of the third pipe 53.

図4は、散気装置30の制御に係るブロック図である。
制御部CONTは、散気管13の空気噴出口8及び開口3bから空気を散気する散気工程あるいは、散気工程とは別に散気管13を洗浄する洗浄工程に応じて、図4に示すように、ブロワ32による空気供給、大気開放弁33の開閉、吸引ポンプ17の駆動及び開閉弁42の開閉を制御する。
FIG. 4 is a block diagram relating to the control of the air diffuser 30.
As shown in FIG. 4, the control unit CONT corresponds to an air diffuser step of air-dissipating air from the air outlet 8 and the opening 3b of the air diffuser pipe 13 or a cleaning step of cleaning the air diffuser pipe 13 separately from the air diffuser step. It also controls the air supply by the blower 32, the opening and closing of the air release valve 33, the drive of the suction pump 17, and the opening and closing of the on-off valve 42.

上記の水処理装置1においては、水槽11内に対して膜モジュール12及び散気装置30等を設置(準備)した後に、散気工程及び洗浄工程が順次行われる。
散気工程は、下記の[表1]におけるタイミングT0に示すように、制御部CONTが大気開放弁33及び開閉弁42を閉塞し、吸引ポンプ17及びブロワ32を駆動(ON)することにより行われる。ブロワ32から供給された空気は、給気管31を介して散気管31の主配管2の内部に流入し、空気噴出口8及び開口3bから噴出して散気される。空気噴出口8及び開口3bから空気を噴出すると、噴出した空気は気泡となり、水槽11中を上昇する。上昇した気泡は、水槽11内の被処理液を伴うことで気液混合流を形成する。この気液混合流は、膜モジュール12に当たることによって各膜エレメント(図示せず)の表面に付着した汚泥等の懸濁物質を剥離する。
In the above water treatment device 1, after installing (preparing) the membrane module 12, the air diffuser 30, and the like in the water tank 11, the air diffuser step and the cleaning step are sequentially performed.
As shown in the timing T0 in [Table 1] below, the air dissipating step is performed by the control unit CONT closing the air release valve 33 and the on-off valve 42 and driving (ON) the suction pump 17 and the blower 32. Will be. The air supplied from the blower 32 flows into the inside of the main pipe 2 of the air diffuser pipe 31 through the air supply pipe 31, and is ejected from the air outlet 8 and the opening 3b to be dispersed. When air is ejected from the air ejection port 8 and the opening 3b, the ejected air becomes bubbles and rises in the water tank 11. The raised bubbles form a gas-liquid mixed flow by being accompanied by the liquid to be treated in the water tank 11. This gas-liquid mixed flow peels off suspended solids such as sludge adhering to the surface of each membrane element (not shown) by hitting the membrane module 12.

洗浄工程は、散気管13の内部を大気開放して水槽11内の液体を散気管13の内部に充満させる充満工程と、散気管13の内部に流入した液体を排出管41を介して排出する排出工程とを含む。より詳細には、制御部CONTは、散気工程の後に充満工程を実施させ、その後に散気工程を実施する第1モードと、散気工程の後に充満工程及び排出工程を実施させ、その後に散気工程を実施させる第2モードとを、予め設定された頻度で切り替えて行わせる。以下、充満工程、排出工程、第1モード及び第2モードについて、[表1]及び[表2]を用いて説明する。 The cleaning step includes a filling step of opening the inside of the air diffuser pipe 13 to the atmosphere to fill the inside of the water tank 11 with the liquid in the water tank 11, and discharging the liquid flowing into the air diffuser pipe 13 through the discharge pipe 41. Includes discharge process. More specifically, the control unit CONT has a first mode in which the filling process is performed after the air dissipating step and then the air dissipating step, and a filling step and the discharging process are performed after the air dissipating step, and then. The second mode in which the air diffusion process is performed is switched at a preset frequency. Hereinafter, the filling process, the discharging process, the first mode and the second mode will be described with reference to [Table 1] and [Table 2].

Figure 0006918667
Figure 0006918667

<充満工程>
充満工程は、上記の[表1]におけるタイミングT1に示すように、制御部CONTが開閉弁42を閉塞した状態で大気開放弁33を開放し、吸引ポンプ17及びブロワ32の駆動を停止(OFF)することにより行われる。ブロワ32の駆動を停止することにより、給気管31を介して散気管13の内部に空気が供給されることが停止される。また、大気開放弁33を開放することにより、散気管13の内部が大気開放される。これにより、散気管13の内部には、空気噴出口8及び開口3bを介して汚泥を含む水槽11内の液体が流入して充満する。
<Filling process>
In the filling step, as shown in the timing T1 in the above [Table 1], the air release valve 33 is opened with the control unit CONT closed the on-off valve 42, and the drive of the suction pump 17 and the blower 32 is stopped (OFF). ) Is done. By stopping the drive of the blower 32, the supply of air to the inside of the air diffuser pipe 13 via the air supply pipe 31 is stopped. Further, by opening the air release valve 33, the inside of the air diffuser pipe 13 is opened to the atmosphere. As a result, the liquid in the water tank 11 containing sludge flows into and fills the inside of the air diffuser pipe 13 through the air outlet 8 and the opening 3b.

第1モードにおいては、[表1]に示されるように、上記タイミングT1の充満工程が完了すると、タイミングT2で上述した散気工程を再開させる。タイミングT2の散気工程開始時には、散気管13の内部が液体で充満しているため、主配管2内等に堆積した堆積物を湿潤状態に保つことができる。また、散気を再開した際に、主配管2内の湿潤状態の堆積物をブロア32からの空気によって空気噴出口8から容易に排出できる。 In the first mode, as shown in [Table 1], when the filling step of the timing T1 is completed, the aeration step described above is restarted at the timing T2. Since the inside of the air diffuser pipe 13 is filled with liquid at the start of the air diffuser process at the timing T2, the deposits accumulated in the main pipe 2 and the like can be kept in a wet state. Further, when the air diffusion is restarted, the wet deposits in the main pipe 2 can be easily discharged from the air outlet 8 by the air from the blower 32.

第1モードは、一例として、大気開放弁33の開放時間が一回あたり10秒以上であり、一日一回以上、24回以下行われる。大気開放弁33の開放時間が一回あたり10秒未満の場合は、散気管13の内部への水槽11内の汚泥を含む液体の流入が不十分である可能性があるが一回あたり10秒以上とすることにより、散気管13の内部に汚泥を含む液体を充満させることが可能になる。第1モードが一日一回未満の場合には、散気管13の洗浄が不十分で主配管2内等に堆積した堆積物を十分に排出できない可能性がある。また、第1モードが一日24回を超えて行われる場合には、水処理効率が低下する可能性がある。そのため、第1モードを実施する頻度としては上記の範囲であることが好ましい。 In the first mode, for example, the opening time of the atmospheric release valve 33 is 10 seconds or more each time, and the first mode is performed once a day or more and 24 times or less. If the opening time of the air release valve 33 is less than 10 seconds each time, there is a possibility that the inflow of the liquid including sludge into the inside of the air diffuser 13 is insufficient, but 10 seconds each time. By doing so, it becomes possible to fill the inside of the air diffuser 13 with a liquid containing sludge. If the first mode is less than once a day, there is a possibility that the air diffuser pipe 13 is not sufficiently cleaned and the deposits accumulated in the main pipe 2 and the like cannot be sufficiently discharged. Further, when the first mode is performed more than 24 times a day, the water treatment efficiency may decrease. Therefore, the frequency of performing the first mode is preferably in the above range.

Figure 0006918667
Figure 0006918667

<排出工程>
排出工程は、上記の[表2]におけるタイミングT2に示すように、上述したタイミングT0(散気工程)及びタイミングT1(充満工程)の後に、制御部CONTが大気開放弁33を閉塞した状態で開閉弁42を開放し、吸引ポンプ17を停止させた状態でブロワ32を駆動(ON)することにより行われる。
<Discharge process>
In the discharge step, as shown in the timing T2 in the above [Table 2], after the timing T0 (air diffusion step) and the timing T1 (filling step) described above, the control unit CONT closes the air release valve 33. This is performed by opening the on-off valve 42 and driving (ON) the blower 32 with the suction pump 17 stopped.

開閉弁42を開放してブロワ32を駆動すると、タイミングT1における大気開放弁33の開放時に散気管13の内部から給気管31内に浸入した汚泥を含む液体が、ブロワ32から供給され空気の圧力により、排出管41に送出される。給気管31及び排出管41は、第3配管53において散気管13の一端側と接続されているため、給気管31内の汚泥を含む液体が排出管41に送出されるのに伴って散気管13内の汚泥を含む液体は一端側から排出管41に送出されて排出され、水槽11内に戻される。散気管13内の汚泥を含む液体が排出されるのに伴って、水槽11内の汚泥を含む液体が空気噴出口8及び開口3bを介して散気管13内に流入しつつ一端側から排出管41に送出され水槽11内に戻される。 When the on-off valve 42 is opened to drive the blower 32, a liquid containing sludge that has entered the air supply pipe 31 from the inside of the air diffuser pipe 13 when the air release valve 33 is opened at the timing T1 is supplied from the blower 32 and the pressure of the air. Is sent to the discharge pipe 41. Since the air supply pipe 31 and the discharge pipe 41 are connected to one end side of the air diffuser pipe 13 in the third pipe 53, the air diffuser pipe is sent as the liquid containing sludge in the air supply pipe 31 is sent to the discharge pipe 41. The liquid containing sludge in 13 is sent from one end side to the discharge pipe 41, discharged, and returned to the water tank 11. As the liquid containing sludge in the air diffuser 13 is discharged, the liquid containing sludge in the water tank 11 flows into the air diffuser 13 through the air outlet 8 and the opening 3b, and is discharged from one end side. It is sent to 41 and returned to the water tank 11.

第2モードにおいては、[表2]に示されるように、上記タイミングT2の排出工程が完了すると、タイミングT3で上述した散気工程を再開させる。タイミングT3の散気工程開始時においても、散気管13の内部が汚泥を含む液体で充満しているため、主配管2内等に堆積した堆積物を湿潤状態に保つことができる。また、散気を再開した際に、主配管2内の湿潤状態の堆積物をブロア32からの空気によって空気噴出口8から容易に排出できる。 In the second mode, as shown in [Table 2], when the discharge step of the timing T2 is completed, the air diffusion step described above is restarted at the timing T3. Even at the start of the air diffuser process at the timing T3, since the inside of the air diffuser pipe 13 is filled with a liquid containing sludge, the deposits accumulated in the main pipe 2 and the like can be kept in a wet state. Further, when the air diffusion is restarted, the wet deposits in the main pipe 2 can be easily discharged from the air outlet 8 by the air from the blower 32.

第2モードは、一例として、開閉弁42の開放時間が一回あたり10秒以上であり、二週間に一回以上、一日一回以下行われる。開閉弁42の開放時間が一回あたり10秒未満の場合は、散気管13の内部の液体の排出が不十分になる可能性があるが一回あたり10秒以上とすることにより、散気管13の内部の汚泥を含む液体を十分に排出することが可能になる。第2モードが二週間に一回未満の場合には、散気管13の洗浄が不十分で主配管2内等に堆積した堆積物を十分に排出できない可能性がある。また、第2モードが一日一回を超えて行われる場合には、水処理効率が低下する可能性がある。そのため、第2モードを実施する頻度としては上記の範囲であることが好ましい。 In the second mode, for example, the opening time of the on-off valve 42 is 10 seconds or more at a time, and is performed once every two weeks or more and once a day or less. If the opening time of the on-off valve 42 is less than 10 seconds at a time, the liquid inside the air diffuser 13 may be insufficiently discharged. It is possible to sufficiently discharge the liquid containing sludge inside the. If the second mode is less than once every two weeks, there is a possibility that the air diffuser pipe 13 is not sufficiently cleaned and the deposits accumulated in the main pipe 2 and the like cannot be sufficiently discharged. Further, if the second mode is performed more than once a day, the water treatment efficiency may decrease. Therefore, the frequency of performing the second mode is preferably in the above range.

第2配管52(排出管41)の管径は、第1配管51(給気管31)の管径の1.1倍以上、2倍以下であることが好ましい。第2配管52の管径が第1配管51の管径の1.1倍未満の場合は、第1配管51を介して供給された空気により、散気管13に充満した汚泥を含む液体を第2配管52を介して円滑に排出することが困難になる可能性がある。第2配管52の管径が第1配管51の管径の2倍を超える場合は、装置の大型化を招くことになってしまう。装置の大型化を招くことなく、散気管13に充満した汚泥を含む液体を第2配管52を介して円滑に排出するためには、第2配管52の管径は、第1配管51の管径に対して上記の範囲であることが好ましい。 The pipe diameter of the second pipe 52 (discharge pipe 41) is preferably 1.1 times or more and 2 times or less the pipe diameter of the first pipe 51 (air supply pipe 31). When the pipe diameter of the second pipe 52 is less than 1.1 times the pipe diameter of the first pipe 51, the air supplied through the first pipe 51 is used to fill the air diffuser pipe 13 with a liquid containing sludge. 2 It may be difficult to discharge smoothly through the pipe 52. If the pipe diameter of the second pipe 52 exceeds twice the pipe diameter of the first pipe 51, the size of the device will be increased. In order to smoothly discharge the liquid containing sludge filled in the air diffuser pipe 13 through the second pipe 52 without inviting an increase in size of the apparatus, the pipe diameter of the second pipe 52 is the pipe of the first pipe 51. It is preferably in the above range with respect to the diameter.

以上のように、本実施形態では、散気管13の内部を大気開放して内部に液体を充満させた後に、散気管13内部の液体を排出管41を介して排出しているため、散気管13内の液体が乾燥することを抑制できる。そのため、本実施形態では、散気管13の目詰まりおよび閉塞を効果的に抑制することができる。また、本実施形態では、給気管31及び排出管41の双方が散気管13の一方側に配置されているため、給気管31と異なる側に排出管41を配置した場合と比較して設置スペースを小さくでき装置の大型化を抑えることが可能になる。加えて、本実施形態では、排出管41を介して排出した液体を水槽11内に戻して水処理するため、排出した液体を貯溜したり処理するための装置を別途設ける必要がなく一層、装置の大型化及び高価格化を抑えることができる。 As described above, in the present embodiment, after the inside of the air diffuser pipe 13 is opened to the atmosphere and the inside is filled with the liquid, the liquid inside the air diffuser pipe 13 is discharged through the discharge pipe 41. Therefore, the air diffuser pipe is discharged. It is possible to prevent the liquid in 13 from drying. Therefore, in the present embodiment, clogging and blockage of the air diffuser 13 can be effectively suppressed. Further, in the present embodiment, since both the air supply pipe 31 and the discharge pipe 41 are arranged on one side of the air diffuser pipe 13, the installation space is compared with the case where the discharge pipe 41 is arranged on a side different from the air supply pipe 31. Can be made smaller and the size of the device can be suppressed. In addition, in the present embodiment, since the liquid discharged through the discharge pipe 41 is returned to the water tank 11 for water treatment, it is not necessary to separately provide a device for storing or treating the discharged liquid. It is possible to suppress the increase in size and price.

また、本実施形態では、給気管31と排出管41とが直結されているため、排出管41内の汚泥を含む液体を、給気管31を介して供給した空気によって効果的に排出することが可能になる。そのため、本実施形態では、汚泥を含む液体の汚泥粘度が高い場合(例えば、MLSS(Mixed Liquor Suspended Solids:活性汚泥浮遊物質)で12,000mg/L以上)であっても支障なく排出管41を介して排出することができる。 Further, in the present embodiment, since the air supply pipe 31 and the discharge pipe 41 are directly connected, the liquid containing sludge in the discharge pipe 41 can be effectively discharged by the air supplied through the air supply pipe 31. It will be possible. Therefore, in the present embodiment, even when the sludge viscosity of the liquid containing sludge is high (for example, 12,000 mg / L or more in MLSS (Mixed Liquor Suspended Solids)), the discharge pipe 41 can be used without any problem. Can be discharged through.

以上、添付図面を参照しながら本発明に係る好適な実施形態について説明したが、本発明は係る例に限定されないことは言うまでもない。上述した例において示した各構成部材の諸形状や組み合わせ等は一例であって、本発明の主旨から逸脱しない範囲において設計要求等に基づき種々変更可能である。 Although the preferred embodiments according to the present invention have been described above with reference to the accompanying drawings, it goes without saying that the present invention is not limited to the above examples. The various shapes and combinations of the constituent members shown in the above-mentioned examples are examples, and can be variously changed based on design requirements and the like within a range that does not deviate from the gist of the present invention.

例えば、上記実施形態では、給気管31と排出管41とが直結され、給気管31と排出管41との接続部に散気管13が接続される構成を例示したが、この構成に限定されない。例えば、散気管13の長さ方向の中途に、当該長さ方向と直交する方向の一方側に給気管31が接続され、他方側に排出管41が接続される構成であってもよい。 For example, in the above embodiment, the configuration in which the air supply pipe 31 and the discharge pipe 41 are directly connected and the air diffuser pipe 13 is connected to the connection portion between the air supply pipe 31 and the discharge pipe 41 is illustrated, but the configuration is not limited to this configuration. For example, the air supply pipe 31 may be connected to one side in the direction orthogonal to the length direction and the discharge pipe 41 may be connected to the other side in the middle of the length direction of the air diffuser pipe 13.

また、上記実施形態では、排出管41を介して排出した液体を水槽11内に戻す構成を例示したが、この構成に限定されず、例えば外部に排出する構成としてもよい。 Further, in the above embodiment, the configuration in which the liquid discharged through the discharge pipe 41 is returned to the inside of the water tank 11 is illustrated, but the configuration is not limited to this configuration, and for example, the configuration may be such that the liquid is discharged to the outside.

また、上記実施形態では、水槽11内に膜モジュール12が配置され、汚泥含有水を膜濾過して、汚泥と透過水(処理水)とを膜分離(固液分離)する構成を例示したが、この構成に限定されない。例えば、曝気と曝気停止とを繰り返して、活性汚泥の作用により工業排水などの被処理水を生物処理する曝気槽にも適用可能である。 Further, in the above embodiment, the membrane module 12 is arranged in the water tank 11, the sludge-containing water is membrane-filtered, and the sludge and the permeated water (treated water) are separated by a membrane (solid-liquid separation). , Not limited to this configuration. For example, it can be applied to an aeration tank in which aeration and aeration stop are repeated to biologically treat water to be treated such as industrial wastewater by the action of activated sludge.

11…水槽、 13…散気管、 30…散気装置、 31…給気管、 33…大気開放弁、 排出管…41、 42…開閉弁、 51…第1配管、 52…第2配管、 53…第3配管 11 ... water tank, 13 ... air diffuser, 30 ... air diffuser, 31 ... air supply pipe, 33 ... air release valve, discharge pipe ... 41, 42 ... on-off valve, 51 ... first pipe, 52 ... second pipe, 53 ... Third pipe

Claims (7)

水槽内に浸漬した散気管に給気管から空気を供給し、前記散気管の空気噴出口から空気を散気する散気工程が行われる散気装置の洗浄方法であって、
大気開放弁が設けられ前記散気管の一端側に接続した前記給気管と、
開閉弁が設けられ前記散気管の一端側に接続した排出管とを準備する工程と、
前記開閉弁を閉塞するとともに前記給気管からの空気の供給を停止した状態で、前記大気開放弁を開放して前記散気管の内部を大気開放し、前記空気噴出口を介して前記水槽内の液体を前記散気管の内部に充満させる充満工程と、
前記大気開放弁を閉塞するとともに前記開閉弁を開放した状態で、前記給気管から空気を供給して前記散気管の一端側を介して前記排出管に送出することにより、前記空気噴出口を介して前記給気管の内部に流入した液体を前記排出管を介して排出する排出工程と、
を含み、
前記充満工程の後に前記散気工程を行う第1モードと、
前記充満工程の後に前記排出工程及び前記散気工程を順次行う第2モードとを含む散気装置の洗浄方法。
It is a cleaning method of an air diffuser in which an air diffuser step of supplying air from an air supply pipe to an air diffuser tube immersed in a water tank and air-dissipating air from an air outlet of the air diffuser is performed.
The air supply pipe provided with an air release valve and connected to one end side of the air diffuser pipe,
A step of preparing a discharge pipe provided with an on-off valve and connected to one end side of the air diffuser pipe, and
With the on-off valve closed and the air supply from the air supply pipe stopped, the air release valve is opened to open the inside of the air diffuser pipe to the atmosphere, and the inside of the water tank is opened via the air outlet. The filling process of filling the inside of the air diffuser with liquid,
With the air release valve closed and the on-off valve open, air is supplied from the air supply pipe and sent out to the discharge pipe via one end side of the air diffuser pipe, thereby passing through the air outlet. And the discharge process of discharging the liquid that has flowed into the inside of the air supply pipe through the discharge pipe.
Only including,
A first mode in which the air diffusion step is performed after the filling step, and
A method for cleaning an air diffuser, which includes a second mode in which the discharge step and the air diffuser step are sequentially performed after the filling step.
前記第1モードは、前記大気開放弁の開放時間が一回あたり10秒以上であり、一日一回以上、24回以下行われる請求項記載の散気装置の洗浄方法。 The first mode, the opening time of the atmosphere release valve is not less than 10 seconds per once, once a day or more, a cleaning method of an air diffuser according to claim 1, wherein the performed below 24 times. 前記第2モードは、前記開閉弁の開放時間が10秒以上であり、二週間に一回以上、一日一回以下行われる請求項1または2記載の散気装置の洗浄方法。 The method for cleaning an air diffuser according to claim 1 or 2 , wherein the second mode has an opening time of the on-off valve of 10 seconds or more, and is performed once every two weeks or more and once a day or less. 前記排出管の管径は、給気管の管径の1.1倍以上、2倍以下である請求項1からのいずれか一項に記載の散気装置の洗浄方法。 The method for cleaning an air diffuser according to any one of claims 1 to 3 , wherein the diameter of the discharge pipe is 1.1 times or more and 2 times or less the diameter of the air supply pipe. 前記散気装置は、鉛直方向に延び間隔をあけて配置された第1配管及び第2配管と、前記第1配管及び前記第2配管の下端同士を接続し前記散気管の一端側が中途に接続された第3配管とを有し、
前記第1配管と、前記第3配管の前記散気管との接続部よりも長さ方向の一方側とは、前記給気管を形成し、
前記第2配管と、前記第3配管の前記散気管との接続部よりも長さ方向の他方側とは、前記排出管を形成する請求項1からのいずれか一項に記載の散気装置の洗浄方法。
The air diffuser connects the first pipe and the second pipe arranged in the vertical direction at intervals and the lower ends of the first pipe and the second pipe, and one end side of the air diffuser is connected halfway. Has a plumb bob with a third pipe
The air supply pipe is formed by the first pipe and one side of the third pipe in the length direction with respect to the connection portion between the air diffuser pipe and the air diffuser pipe.
The air diffuser according to any one of claims 1 to 4 , wherein the second pipe and the other side of the third pipe in the length direction from the connection portion of the air diffuser pipe form the discharge pipe. How to clean the equipment.
水槽内に浸漬され空気噴出口を有する散気管を備えた散気装置であって、
大気開放弁が設けられ前記散気管の一端側に接続され前記散気管に空気を供給可能な給気管と、
開閉弁が設けられ前記散気管の一端側に接続され前記散気管の内部に流入した液体を排出可能な排出管と
前記給気管から前記散気管への空気の供給および空気の供給停止と、前記大気開放弁の開閉と、前記開閉弁の開閉とを制御する制御部と、を備え、
前記制御部は、
前記大気開放弁及び前記開閉弁を閉塞した状態で前記散気管に前記給気管から空気を供給させ前記空気噴出口から空気を散気させる散気モードと、
前記開閉弁を閉塞するとともに前記給気管からの空気の供給を停止した状態で、前記大気開放弁を開放して前記散気管の内部を大気開放し、前記空気噴出口を介して前記水槽内の液体を前記散気管の内部に充満させる充満モードと、
前記充満モードの実施後に、前記大気開放弁を閉塞するとともに前記開閉弁を開放した状態で、前記給気管から空気を供給して前記散気管の一端側を介して前記排出管に送出することにより、前記空気噴出口を介して前記給気管の内部に流入した液体を前記排出管を介して排出させる排出モードと、を含み、
前記制御部は、さらに、
前記充満モードの実施後に前記散気モードを実施させる第1モードと、
前記充満モードの実施後に前記排出モード及び前記散気モードを実施させる第2モードと、を切り替える散気装置。
An air diffuser equipped with an air diffuser that is immersed in a water tank and has an air outlet.
An air supply pipe provided with an air release valve and connected to one end side of the air diffuser pipe to supply air to the air diffuser pipe.
A discharge pipe provided with an on-off valve and connected to one end side of the air diffuser pipe to discharge the liquid flowing into the air diffuser pipe .
A control unit for controlling the supply and stop of air supply from the air supply pipe to the air diffuser pipe, the opening and closing of the atmospheric release valve, and the opening and closing of the on-off valve is provided.
The control unit
An air diffuser mode in which air is supplied from the air supply pipe to the air diffuser pipe with the air release valve and the on-off valve closed, and air is diffused from the air outlet.
In a state where the on-off valve is closed and the supply of air from the air supply pipe is stopped, the air release valve is opened to open the inside of the air diffuser pipe to the atmosphere, and the inside of the water tank is opened via the air outlet. A filling mode that fills the inside of the air diffuser with liquid,
After the filling mode is executed, the air is supplied from the air supply pipe and sent to the discharge pipe via one end side of the air diffuser pipe in a state where the air release valve is closed and the on-off valve is open. , A discharge mode in which the liquid that has flowed into the inside of the air supply pipe through the air outlet is discharged through the discharge pipe.
The control unit further
A first mode in which the air diffuser mode is executed after the charge mode is executed, and
An air diffuser that switches between the discharge mode and the second mode in which the air diffuser mode is executed after the charge mode is executed.
鉛直方向に延び間隔をあけて配置された第1配管及び第2配管と、
前記第1配管及び前記第2配管の下端同士を接続し前記散気管の一端側が中途に接続された第3配管とを有し、
前記第1配管と、前記第3配管の前記散気管との接続部よりも長さ方向の一方側とは、前記給気管を形成し、
前記第2配管と、前記第3配管の前記散気管との接続部よりも長さ方向の他方側とは、前記排出管を形成する請求項記載の散気装置。
The first and second pipes that extend in the vertical direction and are arranged at intervals,
It has a third pipe in which the lower ends of the first pipe and the second pipe are connected to each other and one end side of the air diffuser pipe is connected in the middle.
The air supply pipe is formed by the first pipe and one side of the third pipe in the length direction with respect to the connection portion between the air diffuser pipe and the air diffuser pipe.
The air diffuser according to claim 6 , wherein the second pipe and the other side of the third pipe in the length direction from the connection portion of the air diffuser form the discharge pipe.
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