JP2005138016A - Washing method of aeration device - Google Patents

Washing method of aeration device Download PDF

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JP2005138016A
JP2005138016A JP2003376338A JP2003376338A JP2005138016A JP 2005138016 A JP2005138016 A JP 2005138016A JP 2003376338 A JP2003376338 A JP 2003376338A JP 2003376338 A JP2003376338 A JP 2003376338A JP 2005138016 A JP2005138016 A JP 2005138016A
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pipe
air
tank
liquid
valve
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JP4274903B2 (en
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Tatsuya Uejima
達也 上島
Yasunobu Okajima
康信 岡島
Yutaka Yamada
山田  豊
Masaaki Nagano
昌章 永野
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Kubota Corp
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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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Abstract

<P>PROBLEM TO BE SOLVED: To provide a washing method of an aeration device which can bring out an washing effect on the whole of an aeration pipe, prevent the clogging of the aeration pipe for a long time, and perform a stable aeration even in high-concentration activated sludge. <P>SOLUTION: In the aeration device for supplying air from an air supply and exhaust pipe 58 connected to one side of the aeration pipe 55 immersed in a tank to diffuse air from a plurality of air spout openings 67 formed in the bottom of the aeration pipe 55, after stopping air supply to the aeration pipe 55 to fill the aeration pipe 55 with tank liquid flowing backward from the air spout openings 67, air is supplied to the aeration pipe 55 in the state where a valve 65 of the air supply and exhaust pipe 59 connected to the other side of the aeration pipe 55 is closed, the supplied air is discharged together with tank mixed liquid through an air supply and exhaust pipe 59, the tank liquid is made to flow backward from the air spout openings 67 into the aeration pipe 55 to wash the aeration pipe 55, and the washing is intermittently repeated by using a pulsing motion caused by a pressure change in the pipe. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、散気装置の洗浄方法に関し、膜分離活性汚泥法等において槽内混合液を曝気する技術に係るものである。   The present invention relates to a method for cleaning an air diffuser and relates to a technique for aeration of a mixed liquid in a tank in a membrane separation activated sludge method or the like.

従来、膜分離活性汚泥法においては、曝気槽内に浸漬した膜分離装置の下方に散気装置を配置し、散気装置から散気する空気によって曝気槽内の活性汚泥を含む槽内混合液を曝気しており、散気した空気の上昇によって生じる固気液混相の上向流によって膜分離装置の膜面を洗浄している。   Conventionally, in the membrane separation activated sludge method, an air diffuser is disposed below the membrane separator immersed in the aeration tank, and the mixed liquid in the tank containing activated sludge in the aeration tank by the air diffused from the air diffuser The membrane surface of the membrane separation device is washed by the upward flow of the solid-gas / liquid mixed phase generated by the rise of the diffused air.

この膜分離活性汚泥法において使用する散気装置としては、特許文献1に記載するものがある。図3に示すように、曝気槽1の内部には散気装置2と散気装置2の上部に配置する膜分離装置3を浸漬しており、膜分離装置3は分離膜として有機平膜形のものを使用した複数の膜カートリッジを鉛直方向に沿って、かつ所定間隔をあけて平行に配置したもので、隣接する膜カートリッジ間に流路を形成している。各膜カートリッジは膜透過液流路(図示省略)に連通し、槽内の水頭(重力)もしくはポンプ吸引圧を駆動圧として作動する。   As an air diffuser used in the membrane separation activated sludge method, there is one described in Patent Document 1. As shown in FIG. 3, a diffuser 2 and a membrane separation device 3 disposed above the diffuser 2 are immersed in the aeration tank 1, and the membrane separator 3 is an organic flat membrane type as a separation membrane. A plurality of membrane cartridges using those are arranged in parallel in the vertical direction with a predetermined interval, and a flow path is formed between adjacent membrane cartridges. Each membrane cartridge communicates with a membrane permeate flow path (not shown) and operates with the water head (gravity) in the tank or the pump suction pressure as the driving pressure.

散気装置2は膜分離装置3の下方領域を囲む散気ケース4と散気ケース4の下方に配置する散気管5とを有しており、散気管5は水平方向に配置した所定口径の大径管からなる幹配管6と、幹配管6の下方に配置した所定口径の小径管からなる複数の枝配管7とからなる。   The air diffuser 2 has an air diffuser case 4 surrounding a lower region of the membrane separation device 3 and an air diffuser pipe 5 disposed below the air diffuser case 4. The air diffuser 5 has a predetermined diameter arranged in the horizontal direction. It consists of a main pipe 6 made of a large diameter pipe and a plurality of branch pipes 7 made of a small diameter pipe having a predetermined diameter arranged below the main pipe 6.

幹配管6は基端側が空気供給源であるブロア8に連通しており、先端側に散気ドレン管9を接続している。枝配管7は逆T字形をなし、上部の一端で幹配管6に連通するとともに、下部の両端が幹配管6の下方位置で空気噴出口10として開口している。   The trunk pipe 6 communicates with the blower 8 serving as an air supply source on the proximal end side, and an aeration drain pipe 9 is connected to the distal end side. The branch pipe 7 has an inverted T-shape and communicates with the main pipe 6 at one upper end, and both lower ends open as air jets 10 at positions below the main pipe 6.

散気ドレン管9は先端側が幹配管6の上方位置で排気口11として開口しており、途中にドレンバルブ12を設けている。本実施の形態では排気口11が水面上の大気圧下に開口しているが、排気口11を水面下に配置することも可能である。   The diffused drain pipe 9 is open at the tip side as an exhaust port 11 at a position above the main pipe 6 and is provided with a drain valve 12 in the middle. In the present embodiment, the exhaust port 11 is opened under atmospheric pressure on the water surface, but the exhaust port 11 may be disposed below the water surface.

この構成では、通常の散気運転時において、ドレンバルブ12は閉栓した状態にあり、ブロア8から供給する空気が幹配管6を通って各枝配管7の空気噴出口10から曝気槽1の槽内混合液中に噴出する。   In this configuration, during normal aeration operation, the drain valve 12 is in a closed state, and the air supplied from the blower 8 passes through the main pipe 6 and from the air outlet 10 of each branch pipe 7 to the tank of the aeration tank 1. It spouts into the inner mixed liquid.

散気した空気は槽内混合液を曝気するとともに、その上昇によって固気液混相の上向流を生起する。この上向流は槽内混合液を攪拌混合し、膜分離装置3の各膜カートリッジ間の流路に槽内混合液をクロスフローで供給する。膜分離装置3は槽内混合液を各膜カートリッジの濾過膜を通して濾過し、上向流が膜面に沿って掃流として流れ、各膜カートリッジの膜面にケーキが付着することを抑制する。   The diffused air aerates the mixed liquid in the tank, and ascends to cause an upward flow of the solid-gas mixed phase. This upward flow stirs and mixes the mixed liquid in the tank, and supplies the mixed liquid in the tank to the flow path between the membrane cartridges of the membrane separation device 3 by cross flow. The membrane separation device 3 filters the mixed liquid in the tank through the filtration membrane of each membrane cartridge, and the upward flow flows as a sweep along the membrane surface, thereby suppressing the cake from adhering to the membrane surface of each membrane cartridge.

洗浄運転時には、幹配管6にブロア8から所定圧力の空気を供給する状態でドレンバルブ12を開栓し、幹配管6に供給する空気を散気ドレン管9を通して排気口11から大気圧下に排気する。   During the cleaning operation, the drain valve 12 is opened while air of a predetermined pressure is supplied from the blower 8 to the main pipe 6, and the air supplied to the main pipe 6 is discharged from the exhaust port 11 to the atmospheric pressure through the diffused drain pipe 9. Exhaust.

このとき、槽内混合液が枝配管7を通して幹配管6の内部に逆流入し、逆流入した槽内混合液は枝配管7と幹配管6の内部に付着した汚泥を洗い流して洗浄し、幹配管6を流れる空気とともに散気ドレン管9を通って排気口11から排出される。枝配管7と幹配管6の内部に付着した汚泥は散気時の空気によって乾燥しているが、槽内混合液が汚泥に浸潤することで汚泥の剥離が促進される。   At this time, the mixed liquid in the tank flows back into the trunk pipe 6 through the branch pipe 7, and the mixed liquid in the tank that has flowed in reversely rinses and cleans sludge adhering to the inside of the branch pipe 7 and the trunk pipe 6. Together with the air flowing through the pipe 6, the air is discharged from the exhaust port 11 through the diffused drain pipe 9. Sludge adhering to the inside of the branch pipe 7 and the trunk pipe 6 is dried by the air at the time of air diffusion, but peeling of the sludge is promoted by infiltration of the mixed liquid in the tank into the sludge.

散気ドレン管9内における気液混相流の液相と気相のバランスは槽内液の流入量によって変化し、流入量が増加するのに伴って液相が抵抗として作用し、排気空気によって槽内液を連行することが困難となり、散気ドレン管9内に滞留する槽内液が増加して排気が阻害される。   The balance between the liquid phase and the gas phase of the gas-liquid mixed phase flow in the diffuser drain pipe 9 changes depending on the inflow amount of the liquid in the tank, and the liquid phase acts as a resistance as the inflow amount increases, It becomes difficult to entrain the liquid in the tank, and the liquid in the tank staying in the diffuser drain pipe 9 increases, and the exhaust is inhibited.

この槽内液による阻害によって幹配管6および散気ドレン管9に脈動が生じ、この脈動によって空気噴出口10から枝配管7および幹配管6へ流入する槽内液を散気ドレン管9から排出する洗浄状態と、散気ドレン管9内に滞留する槽内液に阻害されて空気が空気噴出口10から噴出する散気状態とが断続的に反復して繰り返される。この枝配管7への急速な槽内混合液の流入が反復的に生じることで、手動や制御機器による弁の開閉の繰り返し操作を行なうことなく、枝配管7の内部に付着した汚泥を繰り返し洗浄し、汚泥を効果的に除去することができる。
特開2002−166290公報
Inhibition by the liquid in the tank causes pulsation in the main pipe 6 and the diffused drain pipe 9, and the liquid in the tank flowing into the branch pipe 7 and the main pipe 6 from the air outlet 10 is discharged from the diffused drain pipe 9 by this pulsation. The cleaning state to be performed and the diffused state in which air is ejected from the air outlet 10 by being inhibited by the liquid in the tank staying in the diffuser drain tube 9 are repeated repeatedly. The rapid inflow of the mixed liquid in the tank to the branch pipe 7 repeatedly causes the sludge adhering to the inside of the branch pipe 7 to be repeatedly washed without repeating manual valve opening and closing operations by a control device. And sludge can be effectively removed.
JP 2002-166290 A

しかし、上記した構成において、槽内液は空気噴出口10から枝配管7および幹配管6へ流入し、幹配管6の下流側から散気ドレン管9へ流入するので、上流側ほど洗浄効果が弱くなり、最上流側に位置する枝配管7より上流側の散気管5の内部には槽内液が流入せず、その洗浄効果を与えることができない。   However, in the above configuration, the liquid in the tank flows into the branch pipe 7 and the trunk pipe 6 from the air outlet 10 and flows into the diffuser drain pipe 9 from the downstream side of the trunk pipe 6, so that the upstream side has a cleaning effect. The liquid in the tank does not flow into the diffuser pipe 5 on the upstream side of the branch pipe 7 positioned on the most upstream side, and the cleaning effect cannot be given.

散気管5が部分的に閉塞すると幹配管6への空気の流入抵抗が増大し、各枝配管7の空気噴出口10から均一に散気することが困難となる。
本発明は上記した課題を解決するものであり、洗浄効果を散気管の全体に及ぼすことができ、長期にわたり散気管の閉塞を防ぐことができ、高濃度の活性汚泥中においても安定した散気を行うことができる散気装置の洗浄方法を提供することを目的とする。
When the diffuser pipe 5 is partially blocked, the inflow resistance of air to the trunk pipe 6 increases, and it becomes difficult to uniformly diffuse air from the air outlet 10 of each branch pipe 7.
The present invention solves the above-described problems, can exert a cleaning effect on the entire diffuser, can prevent the obstruction of the diffuser over a long period of time, and is stable even in a high concentration activated sludge. It is an object of the present invention to provide a method for cleaning an air diffuser capable of performing the above.

上記した課題を解決するために、本発明の請求項1に記載する散気装置の洗浄方法は、槽内に浸漬した配管の一側から空気を供給し、配管の下部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、配管への空気供給を停止して空気噴出口から逆流する槽内液を配管内に充たした後に、配管の他側に設けたバルブを開栓する状態で配管へ空気を供給し、供給した空気を槽内液とともに配管の他側の排出口を通して排出し、空気噴出口から配管内に槽内液を逆流入させて配管を洗浄し、配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洗浄を繰り返すものである。   In order to solve the above-described problem, a method of cleaning an air diffuser according to claim 1 of the present invention is a method of supplying air from one side of a pipe immersed in a tank and providing a plurality of air provided at the lower part of the pipe In an air diffuser that diffuses air from the jet outlet, after the air supply to the pipe is stopped and the liquid in the tank flowing backward from the air jet outlet is filled in the pipe, the valve provided on the other side of the pipe is opened. Air is supplied to the pipe in a state of being discharged, and the supplied air is discharged together with the liquid in the tank through the discharge port on the other side of the pipe, and the liquid in the tank is reversely flowed into the pipe from the air outlet to clean the pipe. Washing is repeated intermittently by utilizing the pulsation caused by the pressure change inside.

上記した構成により、断続的に洗浄を繰り返す前に、空気供給源のブロア等を停止し、空気噴出口から逆流する槽内液を配管内に充たすことで、空気の流れ方向で最上流に位置する空気噴出口より上流側の配管内にも槽内液が行き渡り、配管の内部に付着した汚泥は散気時の空気によって乾燥しているが、槽内混合液が汚泥に浸潤することで汚泥の剥離を容易化し、次工程の洗浄の初期時に槽内液の排出に伴って洗い流すことで、配管の全体の洗浄を行うことができる。   With the configuration described above, before the cleaning is intermittently repeated, the blower of the air supply source is stopped, and the liquid in the tank flowing backward from the air outlet is filled in the pipe, so that it is positioned at the most upstream in the air flow direction. The liquid in the tank spreads in the pipe upstream from the air outlet, and the sludge adhering to the inside of the pipe is dried by the air at the time of air diffusion, but the sludge is infiltrated by the mixed liquid in the tank. The entire piping can be cleaned by facilitating the separation of the pipe and washing away the liquid in the tank at the initial stage of the cleaning in the next step.

洗浄においては、バルブを開栓して配管から排気すると配管内の静圧が低下して空気噴出口から槽内液が流入する。配管内に流入した槽内液は空気とともに気液混相流となって配管の他側の排出口から流れ出る。   In cleaning, when the valve is opened and exhausted from the pipe, the static pressure in the pipe is lowered and the liquid in the tank flows from the air outlet. The liquid in the tank that has flowed into the pipe becomes a gas-liquid mixed phase flow together with air and flows out from the outlet on the other side of the pipe.

このとき、配管内における気液混相流の液相と気相のバランスは槽内液の流入量によって変化し、流入量が増加するのに伴って液相が抵抗として作用し、排気空気によって槽内液を連行することが困難となり、配管内に滞留する槽内液が増加して排気が阻害される。   At this time, the balance between the liquid phase and the gas phase of the gas-liquid mixed phase flow in the pipe changes depending on the inflow amount of the liquid in the tank, and the liquid phase acts as a resistance as the inflow amount increases, and the exhaust air It becomes difficult to entrain the internal liquid, and the liquid in the tank staying in the pipe is increased, and the exhaust is hindered.

この槽内液による阻害によって配管に脈動が生じ、空気噴出口から配管内へ流入する槽内液を配管から排出する洗浄状態が断続的に繰り返し生じ、洗浄を繰り返し行うことで確実な配管の洗浄を行なうことができ、付帯設備として洗浄水タンクや洗浄ポンプが不要となり、メンテナンス作業者の負担を軽減できる。   Pulsation occurs in the pipe due to the inhibition by the liquid in the tank, and the cleaning state in which the liquid in the tank flowing into the pipe from the air outlet is discharged from the pipe is repeatedly and repeatedly performed. This eliminates the need for a washing water tank or washing pump as ancillary equipment, reducing the burden on maintenance workers.

本発明の請求項2に記載する散気装置の洗浄方法は、槽内に浸漬した配管の一側から空気を供給し、配管の下部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、配管への空気供給を停止するとともに、配管の他側に設けたバルブを開栓して空気噴出口から逆流する槽内液を配管内に充たした後に、配管のバルブを開栓する状態で配管へ空気を供給し、供給した空気を槽内液とともに配管の他側の排出口を通して排出し、空気噴出口から配管内に槽内液を逆流入させて配管を洗浄し、配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洗浄を繰り返すものである。   According to a second aspect of the present invention, there is provided a method of cleaning an air diffuser in which air is supplied from one side of a pipe immersed in a tank and air is diffused from a plurality of air jets provided at the lower part of the pipe. In the air device, the air supply to the piping is stopped, the valve provided on the other side of the piping is opened, the tank liquid backflowed from the air outlet is filled in the piping, and then the piping valve is opened. Air is supplied to the pipe in a state of being discharged, and the supplied air is discharged together with the liquid in the tank through the discharge port on the other side of the pipe, and the liquid in the tank is reversely flowed into the pipe from the air outlet to clean the pipe. Washing is repeated intermittently by utilizing the pulsation caused by the pressure change inside.

上記した構成により、配管への空気供給を停止するとともに、配管の他側に接続したバルブを開栓することで、配管内の空気の排気を促進して空気噴出口から槽内液が配管内に逆流することを容易化する。   With the configuration described above, the air supply to the pipe is stopped and the valve connected to the other side of the pipe is opened to promote the exhaust of the air in the pipe so that the liquid in the tank is discharged from the air outlet into the pipe. To facilitate backflow.

本発明の請求項3に記載する散気装置の洗浄方法は、槽内に浸漬した配管の一側から空気を供給し、配管の下部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、配管へ空気を供給する状態で配管の一側に接続したバルブを開栓して配管を大気開放し、空気噴出口から逆流する槽内液を散気管内に充たした後に、配管の一側のバルブを閉栓し、配管の他側に設けたバルブを開栓する状態で配管へ空気を供給し、供給した空気を槽内液とともに配管の他側の排出口を通して排出し、空気噴出口から配管内に槽内液を逆流入させて配管を洗浄し、配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洗浄を繰り返すものである。   According to a third aspect of the present invention, there is provided a method for cleaning an air diffuser, in which air is supplied from one side of a pipe immersed in a tank and air is diffused from a plurality of air jets provided at the lower part of the pipe. In the air device, open the valve connected to one side of the pipe while supplying air to the pipe, open the pipe to the atmosphere, and fill the diffuser pipe with the liquid in the tank flowing backward from the air outlet, then the pipe Air is supplied to the pipe with the valve on the other side closed and the valve provided on the other side of the pipe open, and the supplied air is discharged together with the liquid in the tank through the outlet on the other side of the pipe. The liquid in the tank is caused to flow backward from the jet port into the pipe to wash the pipe, and the washing is repeated intermittently by using the pulsation caused by the pressure change in the pipe.

上記した構成により、配管へ空気を供給する状態で配管の一側に設けたバルブを開栓して配管を大気開放することで、空気供給源から供給する空気が空気噴出口へ到達することなく大気へ放出され、空気供給源から空気を供給する状態を維持しつつ、配管への空気供給を実質的に停止する。よって、空気供給源の起動停止を伴うことなく、バルブ操作によって散気運転、事前注洗浄運転の切り換えを行うことができる。また、空気を供給するブロワを停止する必要がなくなるので、起動・停止の繰り返しによるブロワの劣化を抑制し、ブロワの寿命を延ばすことができる。   With the above-described configuration, the air supplied from the air supply source does not reach the air outlet by opening the valve provided on one side of the pipe while supplying air to the pipe and opening the pipe to the atmosphere. The air supply to the pipe is substantially stopped while maintaining the state of supplying air from the air supply source. Therefore, it is possible to switch between the aeration operation and the pre-cleaning operation by the valve operation without the start and stop of the air supply source. Moreover, since it is not necessary to stop the blower that supplies air, it is possible to suppress the deterioration of the blower due to repeated start-up and stop, and extend the life of the blower.

以上のように本発明によれば、手動操作もしくは自動操作によってバルブを開閉する操作を繰り返さずとも、バルブを一度開栓するだけの簡便な操作によって、配管内に逆流入する槽内液に由来して生じる脈動を利用して散気装置の配管洗浄を繰り返し行なうことができ、洗浄の前に配管内に槽内液を充たすことで、空気の流れ方向で最上流に位置する空気噴出口より上流側の配管内にも槽内液を行き渡らせて汚泥の剥離を容易化し、次工程の洗浄の初期時に槽内液の排出に伴って洗い流すことで配管の全体に洗浄効果を及ぼすことができ、長期にわたり配管の閉塞を防ぐことができ、高濃度の活性汚泥中においても安定した散気を行うことができる。   As described above, according to the present invention, without repeating the operation of opening and closing the valve by manual operation or automatic operation, it is derived from the liquid in the tank that flows back into the pipe by a simple operation of opening the valve once. By using the pulsation that occurs, the pipe cleaning of the air diffuser can be repeated, and by filling the tank with liquid in the tank before cleaning, the air jet outlet located at the most upstream in the air flow direction can be used. It is possible to spread the liquid in the tank also in the upstream pipe to facilitate the separation of sludge, and to wash the drainage of the liquid in the tank at the initial stage of cleaning in the next process. It is possible to prevent the clogging of the piping over a long period of time and perform stable air diffusion even in a high concentration activated sludge.

以下、本発明の実施の形態を図面に基づいて説明する。図1において、曝気槽51の内部には散気装置52と散気装置52の上部に配置する膜分離装置53とを浸漬している。膜分離装置53は曝気槽51に必須のものではないが、本実施の形態に係る膜分離活性汚泥法では活性汚泥の分離手段として使用する。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. In FIG. 1, an aeration device 52 and a membrane separation device 53 disposed above the aeration device 52 are immersed in the aeration tank 51. The membrane separation device 53 is not essential for the aeration tank 51, but is used as a means for separating activated sludge in the membrane separation activated sludge method according to the present embodiment.

膜分離装置53は、例えば有機平膜形、チューブ形、セラミック形の各種の分離膜を使用することができるが、ここでは有機平膜形の分離膜を使用した複数の膜カートリッジを鉛直方向に沿って、かつ所定間隔をあけて平行に配置したものであり、隣接する膜カートリッジ間に流路を形成している。各膜カートリッジは膜透過液流路(図示省略)に連通し、槽内の水頭(重力)もしくはポンプ吸引圧を駆動圧として作動する。   The membrane separation device 53 can use various types of separation membranes such as organic flat membrane type, tube type, and ceramic type. Here, a plurality of membrane cartridges using organic flat membrane type separation membranes are vertically arranged. And arranged in parallel at a predetermined interval, and a flow path is formed between adjacent membrane cartridges. Each membrane cartridge communicates with a membrane permeate flow path (not shown) and operates with the water head (gravity) in the tank or the pump suction pressure as the driving pressure.

散気装置52は膜分離装置53の下方領域を囲む散気ケース54と散気ケース54の下方に配置する散気管55とを有しており、散気管55は水平方向に配置した所定口径の大径管からなる幹配管56と、幹配管56の下方に配置した所定口径の小径管からなる複数の枝配管57とからなる。   The air diffuser 52 has an air diffuser case 54 surrounding a lower region of the membrane separation device 53 and an air diffuser 55 disposed below the air diffuser case 54. The air diffuser 55 has a predetermined diameter arranged in the horizontal direction. It consists of a main pipe 56 made of a large diameter pipe and a plurality of branch pipes 57 made of a small diameter pipe having a predetermined diameter arranged below the main pipe 56.

幹配管56の両側端のそれぞれには第1給排気管(給気管および排気管を兼ねる)58および第2給排気管(給気管および排気管を兼ねる)59が連通しており、散気管55と第1給排気管58および第2給排気管59とで配管を形成している。   A first air supply / exhaust pipe (also serving as an air supply pipe and an exhaust pipe) 58 and a second air supply / exhaust pipe (also serving as an air supply pipe and an exhaust pipe) 59 communicate with each of both side ends of the trunk pipe 56. The first air supply / exhaust pipe 58 and the second air supply / exhaust pipe 59 form a pipe.

第1給排気管58および第2給排気管59は基端が二方に分岐し、それぞれの分岐した一方が空気供給源のブロア60に第1バルブ61および第2バルブ62を介して連通し、第1給排気管58の分岐した他方が第3バルブ63を介して第1排気口64に連通し、第2給排気管59の他方が第4バルブ65を介して第2排気口66に連通している。   The first air supply / exhaust pipe 58 and the second air supply / exhaust pipe 59 branch in two directions at the base end, and one of the branches branches to the air supply source blower 60 via the first valve 61 and the second valve 62. The other branch of the first supply / exhaust pipe 58 communicates with the first exhaust port 64 via the third valve 63, and the other of the second supply / exhaust pipe 59 connects to the second exhaust port 66 via the fourth valve 65. Communicate.

枝配管57は逆T字形をなし、上部の一端で幹配管56に連通するとともに、下部の両端が幹配管56の下方位置で空気噴出口67として開口している。
本実施の形態では第1排気口64および第2排気口66が水面上の大気圧下に開口しているが、第1排気口64および第2排気口66を水面下に配置することも可能である。散気ケース54は図示を省略しているが槽底面に固定している。また、第1バルブ61と第3バルブ63とを一つの三方向弁で置き換え、第2バルブ62と第4バルブ65とを一つの三方向弁で置き換えることも可能である。
The branch pipe 57 has an inverted T-shape and communicates with the main pipe 56 at one upper end, and both lower ends open as air jets 67 at positions below the main pipe 56.
In the present embodiment, the first exhaust port 64 and the second exhaust port 66 are opened under atmospheric pressure on the water surface. However, the first exhaust port 64 and the second exhaust port 66 may be disposed below the water surface. It is. The air diffuser case 54 is fixed to the bottom of the tank, although not shown. It is also possible to replace the first valve 61 and the third valve 63 with a single three-way valve, and replace the second valve 62 and the fourth valve 65 with a single three-way valve.

以下、上記した構成における作用を説明する。通常の散気運転時においては、第1バルブ61と第2バルブ62のどちらか一方を開栓するとともに他方を閉栓し、第3バルブ63、第4バルブ65を閉栓する状態にあるが、ここでは第1バルブ61を開栓し、第2バルブ62、第3バルブ63、第4バルブ65を閉栓する状態で説明する。   Hereinafter, the operation of the above-described configuration will be described. During normal aeration operation, one of the first valve 61 and the second valve 62 is opened and the other is closed, and the third valve 63 and the fourth valve 65 are closed. In the following description, the first valve 61 is opened and the second valve 62, the third valve 63, and the fourth valve 65 are closed.

この状態でブロア60から供給する空気が第1給排気管58を通って幹配管56に流入し、各枝配管57の空気噴出口67から曝気槽51の槽内混合液中に噴出する。
散気した空気は槽内混合液を曝気するとともに、その上昇によって固気液混相の上向流を生起する。この上向流は槽内混合液を攪拌混合し、膜分離装置53の各膜カートリッジ間の流路に槽内混合液をクロスフローで供給する。膜分離装置53は槽内混合液を各膜カートリッジの濾過膜を通して濾過し、上向流が膜面に沿って掃流として流れ、各膜カートリッジの膜面にケーキが付着することを抑制する。
In this state, air supplied from the blower 60 flows into the main pipe 56 through the first air supply / exhaust pipe 58, and is ejected from the air outlet 67 of each branch pipe 57 into the liquid mixture in the aeration tank 51.
The diffused air aerates the mixed liquid in the tank, and the upward flow causes an upward flow of the solid-gas mixed phase. This upward flow stirs and mixes the mixed liquid in the tank, and supplies the mixed liquid in the tank to the flow path between the membrane cartridges of the membrane separation device 53 by crossflow. The membrane separation device 53 filters the mixed liquid in the tank through the filtration membrane of each membrane cartridge, and the upward flow flows as a sweep along the membrane surface, thereby suppressing the cake from adhering to the membrane surface of each membrane cartridge.

洗浄運転時には、洗浄に先立て散気管55に槽内混合液を事前注水する。このため、ブロア60を30秒から10分間程度停止して散気管55への空気供給を停止して空気噴出口67から逆流する槽内混合液を散気管55の内部の全体に充たす。この操作によって、空気の流れ方向で最上流に位置する枝配管57aより上流側の散気管55の内部にも槽内混合液が行き渡り、散気時の空気によって乾燥した状態で散気管55および第1給排気管58の内部に付着している汚泥に槽内混合液が浸潤して汚泥の剥離を容易化し、次工程の洗浄の初期時に槽内混合液の排出に伴って洗い流すことで、散気管55の全体に洗浄効果を及ぼすことができる。   During the cleaning operation, the mixed liquid in the tank is pre-injected into the diffuser 55 prior to cleaning. For this reason, the blower 60 is stopped for about 30 seconds to 10 minutes to stop the air supply to the air diffusing pipe 55 and fill the entire inside of the air diffusing pipe 55 with the liquid mixture in the tank that flows backward from the air outlet 67. By this operation, the mixed liquid in the tank also reaches the inside of the diffuser pipe 55 on the upstream side of the branch pipe 57a positioned at the uppermost stream in the air flow direction, and the diffuser pipe 55 and the second pipe are dried in the air by the air at the time of the diffuser. 1 The mixed liquid in the tank infiltrates into the sludge adhering to the inside of the supply / exhaust pipe 58 to facilitate the separation of the sludge, and by washing away with the discharge of the mixed liquid in the tank at the initial stage of the next process, A cleaning effect can be exerted on the entire trachea 55.

また、事前注水の他の方法としては、ブロア60を停止するとともに、第4バルブ65を開栓して第2給排気管59を第2排気口66で大気開放し、散気管55の内部の空気の排気を促進して空気噴出口67から槽内混合液が散気管55に逆流することを容易化することも可能である。   As another method of pre-water injection, the blower 60 is stopped, the fourth valve 65 is opened, the second air supply / exhaust pipe 59 is opened to the atmosphere through the second exhaust port 66, and the inside of the air diffusion pipe 55 is opened. It is also possible to facilitate the exhaust of air and facilitate the backflow of the mixed liquid in the tank from the air outlet 67 to the diffuser tube 55.

さらに、事前注水の他の方法としては、ブロア60を停止することなく、散気管55へ空気を供給する状態で第3バルブ63を開栓して第1給排気管58を第1排気口64で大気開放することも可能である。この場合にはブロア60から供給する空気が散気管55へ到達することなく大気へ放出され、ブロア60から空気を供給する状態を維持しつつ、散気管55への空気供給を実質的に停止して空気噴出口67から槽内混合液を散気管55に逆流させる。このため、ブロア60の起動停止を伴うことなく、バルブ操作によって散気運転、事前注洗浄運転の切り換えを行うことができる。   Furthermore, as another method of pre-water injection, the third valve 63 is opened and the first air supply / exhaust pipe 58 is connected to the first exhaust port 64 in a state where air is supplied to the diffuser pipe 55 without stopping the blower 60. It is also possible to open to the atmosphere. In this case, the air supplied from the blower 60 is released to the atmosphere without reaching the air diffuser 55, and the air supply to the air diffuser 55 is substantially stopped while maintaining the state of supplying air from the blower 60. Then, the mixed liquid in the tank is caused to flow backward from the air outlet 67 to the diffuser tube 55. For this reason, it is possible to switch between the aeration operation and the pre-cleaning operation by the valve operation without accompanying the start and stop of the blower 60.

事前注水を終えた後に、第1バルブ61、第4バルブ65が開栓された状態で、かつ第2バルブ62、第3バルブ63が閉栓された状態で、ブロア60から第1給排気管58を通して幹配管56に所定圧力の空気を供給し、幹配管56に供給する空気を第2給排気管59を通して第2排気口66から大気圧下に排気する。   After the pre-water injection, the first air supply pipe 58 from the blower 60 in the state where the first valve 61 and the fourth valve 65 are opened and the second valve 62 and the third valve 63 are closed. Air of a predetermined pressure is supplied to the main pipe 56 through the air, and the air supplied to the main pipe 56 is exhausted from the second exhaust port 66 to the atmospheric pressure through the second air supply / exhaust pipe 59.

このとき、第2排気口66が幹配管56の上方位置で大気圧下に開口し、空気噴出口67が幹配管56の下方位置に開口することで、幹配管56における空気の流れの主流がより抵抗の小さい第2排気口66へと向かい、幹配管56に作用する圧力(静圧)が低下し、空気噴出口67に作用する圧力(槽内の水位によって決まる)との圧力差に起因して槽内混合液が枝配管57を通して幹配管56の内部に逆流入する。   At this time, the second exhaust port 66 is opened under atmospheric pressure at a position above the trunk pipe 56, and the air outlet 67 is opened at a position below the trunk pipe 56, so that the main flow of air in the trunk pipe 56 is The pressure (static pressure) acting on the trunk pipe 56 decreases toward the second exhaust port 66 having a smaller resistance, and is caused by the pressure difference from the pressure (determined by the water level in the tank) acting on the air outlet 67. Then, the mixed liquid in the tank flows back into the main pipe 56 through the branch pipe 57.

逆流入した槽内混合液は枝配管57と幹配管56の内部に付着した汚泥を洗い流して洗浄し、幹配管56を流れる空気とともに第2給排気管59を通って第2排気口66から排出される。枝配管57と幹配管56の内部に付着した汚泥は散気時の空気によって乾燥しているが、槽内混合液が汚泥に浸潤することで汚泥の剥離が促進される。   The mixed liquid in the tank that has flowed in reversely washes and removes sludge adhering to the inside of the branch pipe 57 and the trunk pipe 56, and is discharged from the second exhaust port 66 through the second air supply / exhaust pipe 59 together with the air flowing through the trunk pipe 56. Is done. Sludge adhering to the inside of the branch pipe 57 and the trunk pipe 56 is dried by the air at the time of air diffusion, but peeling of the sludge is promoted by infiltration of the mixed liquid in the tank into the sludge.

第2給排気管59における気液混相流の液相と気相のバランスは槽内液の流入量によって変化し、流入量が増加するのに伴って液相が抵抗として作用し、排気空気によって槽内混合液を連行することが困難となり、第2給排気管59に滞留する槽内混合液が増加して排気が阻害される。   The balance between the liquid phase and the gas phase of the gas-liquid mixed phase flow in the second air supply / exhaust pipe 59 changes depending on the inflow amount of the liquid in the tank, and as the inflow amount increases, the liquid phase acts as a resistance. It becomes difficult to entrain the mixed liquid in the tank, and the mixed liquid in the tank staying in the second air supply / exhaust pipe 59 is increased and the exhaust is inhibited.

この槽内混合液による阻害によって幹配管56および第2給排気管59に脈動が生じ、空気噴出口67から枝配管57および幹配管56へ流入する槽内混合液を第2給排気管59を通して第2排気口66から排出する洗浄状態が断続的に反復して繰り返される。   The inhibition by the mixed liquid in the tank causes pulsation in the trunk pipe 56 and the second supply / exhaust pipe 59, and the mixed liquid in the tank flowing into the branch pipe 57 and the trunk pipe 56 from the air outlet 67 passes through the second supply / exhaust pipe 59. The cleaning state discharged from the second exhaust port 66 is repeated repeatedly and intermittently.

この枝配管57への急速な槽内混合液の流入が反復的に生じることで、手動や制御機器による弁の開閉の繰り返し操作を行なうことなく、枝配管57の内部に付着した汚泥を繰り返し洗浄し、汚泥を効果的に除去することができる。   The rapid inflow of the mixed liquid in the tank to the branch pipe 57 repeatedly causes the sludge adhering to the inside of the branch pipe 57 to be repeatedly washed without performing manual and control valve opening / closing operations repeatedly. And sludge can be effectively removed.

上述した洗浄運転において、幹配管56を流れる槽内混合液の流れ方向の最上流側に位置する枝配管57aより上流側の幹配管56の内部における洗浄の効果が十分に得ることができない場合には、第1バルブ61を閉栓するとともに第2バルブ62を開栓し、第3バルブ63、第4バルブ65を閉栓する状態で散気運転を行い、洗浄運転時には、事前注水の後に、ブロア60から第2給排気管59を通して幹配管56に所定圧力の空気を供給する状態で第3バルブ63を開栓し、幹配管56に供給する空気を第1給排気管58を通して第1排気口64から大気圧下に排気し、空気噴出口67から枝配管57および幹配管56へ流入する槽内混合液を第1給排気管58を通して第1排気口64から排出する洗浄状態を脈動によって断続的に反復して繰り返させる。この操作によって、散気管55の全体に洗浄効果が及ぶ。   In the above-described cleaning operation, when the effect of cleaning inside the main pipe 56 upstream from the branch pipe 57a located on the most upstream side in the flow direction of the mixed liquid in the tank flowing through the main pipe 56 cannot be sufficiently obtained. Performs the aeration operation with the first valve 61 closed and the second valve 62 opened, and the third valve 63 and the fourth valve 65 closed. The third valve 63 is opened in a state where air of a predetermined pressure is supplied to the main pipe 56 from the second supply / exhaust pipe 59 to the first exhaust port 64 through the first supply / exhaust pipe 58. From the air outlet 67 to the branch pipe 57 and the trunk pipe 56, and the cleaning state in which the mixed liquid in the tank is discharged from the first exhaust port 64 through the first air supply / exhaust pipe 58 is intermittently caused by pulsation. Against To make repeated. By this operation, the entire diffusing tube 55 has a cleaning effect.

このように、一定の周期毎に、例えば洗浄運転のたびに、第1バルブ61、第2バルブ62の開閉操作により散気管55へ通気する管路としての第1給排気管58と第2給排気管59を切り換える操作、第3バルブ63、第4バルブ65の開閉操作により散気管55から排気する管路としての第1給排気管58と第2給排気管59を切り換える操作、および第1排気口64と第2排気口66を切り換える操作を行うことにより、洗浄時に散気管55の内部で槽内混合液が流れる方向および槽内混合液の流れる何れかの給排気管58、59が一定の周期で切り換り、脈動による洗浄効果を散気管55および双方の給排気管58、59の全体に及ぼすことができる。   As described above, the first air supply / exhaust pipe 58 and the second air supply pipe 58 are connected to the air diffusion pipe 55 by opening / closing the first valve 61 and the second valve 62 at regular intervals, for example, every cleaning operation. An operation for switching the exhaust pipe 59, an operation for switching the first air supply / exhaust pipe 58 and the second air supply / exhaust pipe 59 as a pipe line for exhausting from the diffuser pipe 55 by opening / closing the third valve 63 and the fourth valve 65, and the first By performing an operation of switching between the exhaust port 64 and the second exhaust port 66, any of the supply / exhaust pipes 58, 59 in which the mixed liquid in the tank flows and the mixed liquid in the tank flows in the air diffusion pipe 55 at the time of cleaning is constant. Thus, the cleaning effect by pulsation can be exerted on the diffuser pipe 55 and the entire supply / exhaust pipes 58 and 59.

図2に示すように、散気管55はループ状に形成し、中間位置に第1給排気管58と第2給排気管59を接続することも可能である。
また、本発明は先に図1に示す構成においても実施することができ、ブロア8の停止、ドレンバルブ12の開栓操作によって事前注水を行う。あるいは、ブロア8の近傍に別途の配管を分岐してバルブを設け、排気口を形成することで、ブロア8を停止することなく事前注水する操作が可能となる。
As shown in FIG. 2, the air diffusion pipe 55 can be formed in a loop shape, and the first air supply / exhaust pipe 58 and the second air supply / exhaust pipe 59 can be connected to an intermediate position.
The present invention can also be implemented in the configuration shown in FIG. 1, and pre-water injection is performed by stopping the blower 8 and opening the drain valve 12. Alternatively, a separate pipe is branched in the vicinity of the blower 8 and a valve is provided to form an exhaust port, whereby an operation of pre-watering without stopping the blower 8 becomes possible.

本発明の実施の形態における散気装置を示す正面図である。It is a front view which shows the aeration apparatus in embodiment of this invention. 本発明の他の実施の形態における散気管を示す斜視図である。It is a perspective view which shows the diffuser tube in other embodiment of this invention. 従来の散気装置を示す正面図である。It is a front view which shows the conventional diffuser.

符号の説明Explanation of symbols

51 曝気槽
52 散気装置
53 膜分離装置
54 散気ケース
55 散気管
56 幹配管
57 枝配管
58 第1給排気管
59 第2給排気管
60 ブロア
61 第1バルブ
62 第2バルブ
63 第3バルブ
64 第1排気口
65 第4バルブ
66 第2排気口
67 空気噴出口
51 Aeration tank 52 Air diffuser 53 Membrane separation device 54 Air diffuser case 55 Air diffuser pipe 56 Trunk pipe 57 Branch pipe 58 First air supply / exhaust pipe 59 Second air supply / exhaust pipe 60 Blower 61 First valve 62 Second valve 63 Third valve 64 1st exhaust port 65 4th valve 66 2nd exhaust port 67 Air outlet

Claims (3)

槽内に浸漬した配管の一側から空気を供給し、配管の下部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、配管への空気供給を停止して空気噴出口から逆流する槽内液を配管内に充たした後に、配管の他側に設けたバルブを開栓する状態で配管へ空気を供給し、供給した空気を槽内液とともに配管の他側の排出口を通して排出し、空気噴出口から配管内に槽内液を逆流入させて配管を洗浄し、配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洗浄を繰り返すことを特徴とする散気装置の洗浄方法。 In an air diffuser that supplies air from one side of a pipe immersed in the tank and diffuses air from a plurality of air outlets provided in the lower part of the pipe, the air supply to the pipe is stopped and the air outlet is After filling the liquid in the tank that flows back into the pipe, supply air to the pipe with the valve provided on the other side of the pipe open, and the supplied air passes through the outlet on the other side of the pipe along with the liquid in the tank. The liquid is discharged, the liquid in the tank is reversely flowed into the pipe from the air outlet, the pipe is washed, and the washing is intermittently repeated using the pulsation caused by the pressure change in the pipe. Cleaning method of the air device. 槽内に浸漬した配管の一側から空気を供給し、配管の下部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、配管への空気供給を停止するとともに、配管の他側に設けたバルブを開栓して空気噴出口から逆流する槽内液を配管内に充たした後に、配管のバルブを開栓する状態で配管へ空気を供給し、供給した空気を槽内液とともに配管の他側の排出口を通して排出し、空気噴出口から配管内に槽内液を逆流入させて配管を洗浄し、配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洗浄を繰り返すことを特徴とする散気装置の洗浄方法。 In an air diffuser that supplies air from one side of a pipe immersed in the tank and diffuses air from a plurality of air jets provided in the lower part of the pipe, the air supply to the pipe is stopped and After opening the valve provided on the side and filling the pipe with the liquid in the tank that flows backward from the air outlet, air is supplied to the pipe with the pipe valve opened, and the supplied air is supplied to the liquid in the tank. In addition, it is discharged through the discharge port on the other side of the pipe, and the liquid in the tank is reversely flowed into the pipe from the air jet outlet to clean the pipe, and intermittently using the pulsation caused by the pressure change in the pipe A method of cleaning an air diffuser characterized by repeating cleaning. 槽内に浸漬した配管の一側から空気を供給し、配管の下部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、配管へ空気を供給する状態で配管の一側に接続したバルブを開栓して配管を大気開放し、空気噴出口から逆流する槽内液を散気管内に充たした後に、配管の一側のバルブを閉栓し、配管の他側に設けたバルブを開栓する状態で配管へ空気を供給し、供給した空気を槽内液とともに配管の他側の排出口を通して排出し、空気噴出口から配管内に槽内液を逆流入させて配管を洗浄し、配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洗浄を繰り返すことを特徴とする散気装置の洗浄方法。 In an air diffuser that supplies air from one side of a pipe immersed in the tank and diffuses air from a plurality of air jets provided in the lower part of the pipe, the air is supplied to the pipe on one side. A valve provided on the other side of the pipe after opening the connected valve, opening the pipe to the atmosphere, filling the liquid in the tank flowing backward from the air outlet into the diffuser pipe, closing the valve on one side of the pipe Air is supplied to the pipe with the pipe open, the supplied air is discharged together with the liquid in the tank through the other outlet on the pipe, and the liquid in the tank is reversely flowed into the pipe from the air outlet to clean the pipe. And the cleaning method of the air diffuser characterized by repeating washing | cleaning intermittently using the pulsation which originates in the pressure change in piping.
JP2003376338A 2003-11-06 2003-11-06 Cleaning method for air diffuser Expired - Lifetime JP4274903B2 (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006263716A (en) * 2005-02-24 2006-10-05 Toray Ind Inc Dipping type membrane separation apparatus, washing method of air diffuser and membrane separation method
US20100218789A1 (en) * 2009-02-27 2010-09-02 Toray Industries, Inc. Submerged membrane separation apparatus, cleaning method for diffusing apparatus, and method for membrane separation
JP2010207799A (en) * 2009-03-09 2010-09-24 Shenzhen Jdl Environmental Protection Ltd Jet aeration apparatus and method of using the same
JP2011092835A (en) * 2009-10-28 2011-05-12 Mitsubishi Rayon Co Ltd Method for operating aeration device
WO2014061737A1 (en) * 2012-10-19 2014-04-24 三菱レイヨン株式会社 Air diffusion device, air diffusion method, and water treatment device

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006263716A (en) * 2005-02-24 2006-10-05 Toray Ind Inc Dipping type membrane separation apparatus, washing method of air diffuser and membrane separation method
US20100218789A1 (en) * 2009-02-27 2010-09-02 Toray Industries, Inc. Submerged membrane separation apparatus, cleaning method for diffusing apparatus, and method for membrane separation
JP2010194524A (en) * 2009-02-27 2010-09-09 Toray Ind Inc Immersion type membrane separator, washing method of air diffuser, and membrane separation method
US8377225B2 (en) * 2009-02-27 2013-02-19 Toray Industries, Inc. Submerged membrane separation apparatus, cleaning method for diffusing apparatus, and method for membrane separation
JP2010207799A (en) * 2009-03-09 2010-09-24 Shenzhen Jdl Environmental Protection Ltd Jet aeration apparatus and method of using the same
JP2011092835A (en) * 2009-10-28 2011-05-12 Mitsubishi Rayon Co Ltd Method for operating aeration device
WO2014061737A1 (en) * 2012-10-19 2014-04-24 三菱レイヨン株式会社 Air diffusion device, air diffusion method, and water treatment device
JPWO2014061737A1 (en) * 2012-10-19 2016-09-05 三菱レイヨン株式会社 Air diffuser, air diffuser, and water treatment device

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