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JP3784252B2 - Air diffuser - Google Patents

Air diffuser Download PDF

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Publication number
JP3784252B2
JP3784252B2 JP2000389658A JP2000389658A JP3784252B2 JP 3784252 B2 JP3784252 B2 JP 3784252B2 JP 2000389658 A JP2000389658 A JP 2000389658A JP 2000389658 A JP2000389658 A JP 2000389658A JP 3784252 B2 JP3784252 B2 JP 3784252B2
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JP
Japan
Prior art keywords
air
pipe
tank
sludge
diffuser
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
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JP2000389658A
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Japanese (ja)
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JP2002186991A (en
Inventor
康信 岡島
昌章 永野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kubota Corp
Original Assignee
Kubota Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority to JP2000389658A priority Critical patent/JP3784252B2/en
Application filed by Kubota Corp filed Critical Kubota Corp
Priority to AT01999424T priority patent/ATE349271T1/en
Priority to US10/182,564 priority patent/US6843470B2/en
Priority to PCT/JP2001/010297 priority patent/WO2002045833A1/en
Priority to CNB018045073A priority patent/CN1204961C/en
Priority to DE2001625594 priority patent/DE60125594T2/en
Priority to EP01999424A priority patent/EP1358005B1/en
Priority to ES01999424T priority patent/ES2282329T3/en
Priority to KR1020027010060A priority patent/KR100768873B1/en
Priority to AU24103/02A priority patent/AU783464B2/en
Priority to CA 2398460 priority patent/CA2398460C/en
Priority to AU18521/02A priority patent/AU781443B2/en
Priority to CA 2398461 priority patent/CA2398461C/en
Priority to EP20010999419 priority patent/EP1341597A1/en
Priority to US10/182,636 priority patent/US6843908B2/en
Priority to CNB018044522A priority patent/CN1241676C/en
Priority to KR20027010016A priority patent/KR100768841B1/en
Priority to PCT/JP2001/010524 priority patent/WO2002045827A1/en
Publication of JP2002186991A publication Critical patent/JP2002186991A/en
Publication of JP3784252B2 publication Critical patent/JP3784252B2/en
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Activated Sludge Processes (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、散気装置に関し、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。
【0002】
【従来の技術】
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。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、例えば塩化ビニール製の配管の下方に複数のφ10mm程度の穴を開けただけのものがある。
【0003】
ところで、膜分離装置の膜面洗浄には膜カートリッジの1枚当たりで平均10L/min以上の空気供給が必要となるが、曝気空気の分散が均一に行われない場合には、局所的に曝気空気が多い所で膜へ与える負荷が大きくなるために膜寿命の低下につながり、少ない所で十分な洗浄効果を得られないために膜面の汚れが加速される。
【0004】
一方、膜分離活性汚泥法で生物処理に必要な酸素は、活性汚泥への酸素溶解効率をもとに設定された曝気空気量を所定の曝気ブロアで供給することで確保している。この酸素溶解効率を高くすることは曝気ブロアのダウンサイズ、曝気時間の縮小による省電力化となり望ましいことである。
【0005】
このため、散気装置に小径の空気噴出口を複数個所に設けることで、曝気空気の均一な分散と酸素溶解効率の向上を図ることが求められる。
【0006】
【発明が解決しようとする課題】
しかし、散気管内には散気を停止した時に汚泥が管内に流入し、この汚泥が散気時に空気によって乾燥して空気噴出口を閉塞するので、空気噴出口の小径化は汚泥の乾燥による散気管の閉塞(乾燥性汚泥閉塞)が生じ易くなる原因となり、定期的な洗浄によって未然に防ぐことが基本となる。また、夾雑物や流動性が低い汚泥、大きなフロックなどが空気噴出口を塞ぐことが突発的に発生するので、散気管の閉塞を完全に防ぐことは困難である。この場合、次回の定期洗浄によってほとんどの閉塞は解除されるが、その間に強固に付着した乾燥性汚泥閉塞や膜面洗浄不足による膜間の汚泥閉塞を誘発する問題がある。
【0007】
本発明は上記した課題を解決するものであり、構造的に配管の閉塞を抑制することができるとともに、簡便な操作によって配管の洗浄を行なうことができ、小径の気泡を均一に分散して散気することができる散気装置を提供することを目的とする。
【0008】
【課題を解決するための手段】
上記課題を解決するために、本発明の散気装置は、槽内に浸漬して水平方向に配置し、基端側が空気供給源に連通する幹配管と、幹配管に連通するとともに、先端が幹配管の下方位置で開口する複数の枝配管と、一端が幹配管の先端側に連通するとともに、他端が幹配管の上方位置で排気口として開口する散気ドレン管と、散気ドレン管に設けたドレンバルブとを有し、各枝配管は端部に開放口を有し、上面に端部開放口より小口径の複数の空気噴出口を設けたものである。
【0009】
上記した構成により、散気時にはドレンバルブを閉栓した状態で、空気源から所定圧力で供給する空気を幹配管に基端側から通気し、枝配管を通して空気噴出口から散気する。このとき、各空気噴出口は枝配管の上部に位置するので混合液との密度差による空気の浮力によって端部開放口に達するまでに散気する空気の殆どが空気噴出口より噴出する。
【0010】
空気噴出口は小口径であるので噴出する空気の気泡が小径となり、酸素溶解効率が高くなることで空気源のブロア等を小型化して消費電力を低減できる。また、空気噴出口を小口径化することで単位面積当たりに配置する空気噴出口の数を増加させることができ、そのことで空気噴出口の分散度が高まるので曝気空気が均一に散気されて洗浄効果が高まる。
【0011】
夾雑物や流動性が低い汚泥、大きなフロックなどで空気噴出口が突発的に閉塞しても、枝配管の端部開放口から空気が噴出することで所定の曝気空気量を確保して膜面洗浄を継続することができ、次回の定期洗浄までの間に膜面洗浄不足によって膜間の汚泥閉塞が発生することを防止できる。
【0012】
洗浄時には幹配管に空気源から所定圧力の空気を供給する状態でドレンバルブを開栓し、幹配管に供給する空気を散気ドレン管を通して排気口から大気圧下もしくは所定水深下に排気する。
【0013】
このとき、排気口が幹配管の上方位置に開口し、枝配管の端部開放口および空気噴出口が幹配管の下方位置に開口することで、空気噴出口および枝配管の端部開放口と幹配管との圧力差に起因して槽内液が枝配管の端部開放口および空気噴出口を通して枝配管および幹配管内に逆流入し、流入した槽内液は空気とともに散気ドレン管を通って排気口から排出される。
【0014】
この幹配管内の槽内液は空気の通気を阻害する抵抗として作用し、空気の流れが脈動して幹配管内の圧力が急激な増減を繰り返して変化するので、散気ドレン管の排気口から空気と槽内液が断続的に排出されるとともに、枝配管を通して幹配管内に槽内液が断続的に流入する。
【0015】
この枝配管を通した急速な槽内液の流入が反復的に生じることで、枝配管の内部に付着した汚泥を効果的に洗浄する。枝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、槽内液が汚泥に浸潤することで汚泥の剥離を促進し、剥離した汚泥は槽内液とともに空気の排気に伴って排気口から排出する。
【0016】
したがって、ドレンバルブを開栓するだけの簡単な操作によって、枝配管の内部、空気噴出口、端部開放口、幹配管の内部を洗浄できるので、乾燥性汚泥による散気管の閉塞を未然に防止することができ、乾燥性汚泥で閉塞し易い枝配管の空気噴出口を小口径化することが可能となる。
【0017】
【発明の実施の形態】
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〜図4において、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とを浸漬している。膜分離装置3は曝気槽1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固液分離手段として使用する。
【0018】
膜分離装置3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。
【0019】
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。
【0020】
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、幹配管6の下方に位置する両端に開放口10aを有し、上面に端部開放口10aより小口径の複数の空気噴出口10bを設けている。
【0021】
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。散気ケース4は槽底面に固定しており、散気ケース4と槽開口部との間に設けたガイド13に沿って膜分離装置3が昇降可能である。
【0022】
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、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10bから曝気槽1の槽内混合液中に噴出する。このとき、各空気噴出口10bは枝配管7の上部に位置するので混合液との密度差による空気の浮力によって端部開放口10aに達するまでに散気する空気の殆どが空気噴出口10bより噴出する。
【0023】
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。この散気状態において、空気噴出口10bが小口径であるので噴出する空気の気泡は小径となり、酸素溶解効率が高くなることで空気源のブロア8を小型化して消費電力を低減できる。また、空気噴出口10bを小口径化することで単位面積当たりに配置する空気噴出口10bの数を増加させることができ、そのことで空気噴出口10bの分散度が高まるので曝気空気が均一に散気されて洗浄効果が高まる。
【0024】
夾雑物や流動性が低い汚泥、大きなフロックなどで空気噴出口10bが突発的に閉塞しても、枝配管7の端部開放口10aから空気が噴出することで所定の曝気空気量を確保して膜面洗浄を継続することができ、次回の定期洗浄までの間に膜面洗浄不足によって膜間の汚泥閉塞が発生することを防止できる。
【0025】
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。
【0026】
このとき、排気口11が幹配管6の上方位置で大気圧下に開口し、開放口10aおよび空気噴出口10bが幹配管6の下方位置に開口することで、図3に示すように、開放口10aに作用する圧力P0と幹配管6に作用する圧力P1との圧力差に起因して槽内混合液が開放口10a、空気噴出口10bを通して枝配管7および幹配管6の内部に逆流入する。
【0027】
逆流入した槽内混合液は枝配管7の内部に付着した汚泥を洗い流して水洗浄し、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。
【0028】
幹配管6に流入した槽内混合液は空気の通気を阻害する抵抗として作用し、空気の流れが脈動する。特に散気ドレン管9の鉛直部に滞留する槽内混合液が排気を阻害することで幹配管6の圧力が高まり、圧力の高まりによって滞留した槽内混合液が一気に排出されて幹配管6の圧力が低下する。
【0029】
このようにして幹配管6の内部圧力が急激な増減を繰り返して変化することで、散気ドレン管9の排気口11から空気と槽内混合液が交互に断続的に排出されるとともに、枝配管7を通して幹配管6の内部へ槽内混合液が断続的に流入する。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、手動操作や制御機器による繰り返し操作を行なうことなく、枝配管7の内部、開放口10a、空気噴出口10bに付着した汚泥を繰り返し水洗浄し、汚泥を効果的に除去することができる。
【0030】
【発明の効果】
以上のように本発明によれば、ドレンバルブを開栓するだけの簡単な操作によって、枝配管の内部、端部開放口、空気噴出口、幹配管の内部を洗浄できるので、乾燥性汚泥による散気管の閉塞を未然に防止して乾燥性汚泥で閉塞し易い枝配管の空気噴出口を小口径化することが可能となる。この空気噴出口の小口径化により空気の気泡が小径となって酸素溶解効率が高くなるので空気源のブロア等を小型化して消費電力を低減でき、空気噴出口の小口径化で単位面積当たりに配置する空気噴出口の数を増加させて空気噴出口の分散度を高めることができ、曝気空気を均一に散気して洗浄効果を高めることができる。大きなフロックの汚泥などで空気噴出口が突発的に閉塞しても、枝配管の端部開放口から空気が噴出することで所定の曝気空気量を確保して膜面洗浄を継続することができ、次回の定期洗浄までの間に膜面洗浄不足によって膜間の汚泥閉塞が発生することを防止できる。
【図面の簡単な説明】
【図1】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。
【図2】同散気装置の斜視図である。
【図3】同散気装置の要部断面図である。
【図4】同散気装置の要部拡大図である。
【符号の説明】
1 曝気槽
2 散気装置
3 膜分離装置
4 散気ケース
5 散気管
6 幹配管
7 枝配管
8 ブロア
9 散気ドレン管
10a 開放口
10b 空気噴出口
11 排気口
12 ドレンバルブ
13 ガイド
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a 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.
[0002]
[Prior art]
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. As an air diffuser used in this membrane separation activated sludge method, for example, there is one in which a plurality of holes of about φ10 mm are formed below a pipe made of vinyl chloride.
[0003]
By the way, the membrane surface cleaning of the membrane separation device requires an air supply of 10 L / min or more on an average per membrane cartridge. However, when the aeration air is not uniformly distributed, aeration is performed locally. Since the load applied to the film becomes large at a place where there is a lot of air, the life of the film will be shortened.
[0004]
On the other hand, oxygen necessary for biological treatment in the membrane separation activated sludge method is secured by supplying an aeration air amount set based on oxygen dissolution efficiency in the activated sludge with a predetermined aeration blower. Increasing the oxygen dissolution efficiency is desirable because it reduces power consumption by reducing the size of the aeration blower and reducing the aeration time.
[0005]
For this reason, it is required to provide uniform dispersion of aerated air and improve oxygen dissolution efficiency by providing a plurality of small-diameter air outlets in the diffuser.
[0006]
[Problems to be solved by the invention]
However, sludge flows into the air diffuser when the air diffuser stops, and this sludge is dried by the air during the air diffused and closes the air outlet, so the diameter of the air outlet is reduced by sludge drying. It becomes a cause that obstruction | occlusion of a diffuser pipe (drying sludge obstruction | occlusion) becomes easy to occur, and it is fundamental to prevent beforehand by regular cleaning. Moreover, since impurities, low-fluid sludge, large flocs, and the like suddenly occur to block the air outlet, it is difficult to completely prevent the air diffuser from being blocked. In this case, most blockages are released by the next periodic cleaning, but there is a problem inducing dry sludge blockage firmly adhered during that period and sludge blockage between membranes due to insufficient membrane surface cleaning.
[0007]
The present invention solves the above-described problems, and can structurally suppress the clogging of the pipe and can clean the pipe by a simple operation. An object of the present invention is to provide an air diffuser that can be noticed.
[0008]
[Means for Solving the Problems]
In order to solve the above-mentioned problems, the air diffuser of the present invention is immersed in a tank and arranged in a horizontal direction, and the proximal end communicates with the air supply source, the trunk pipe communicates with the trunk pipe, and the distal end is A plurality of branch pipes opened at a position below the main pipe, an air diffuser pipe having one end communicating with the tip end side of the main pipe and the other end opened as an exhaust port above the main pipe, and an air diffuser pipe Each branch pipe has an open port at the end, and a plurality of air jets having a smaller diameter than the end open port are provided on the upper surface.
[0009]
With the above configuration, when air is diffused, the air supplied from the air source at a predetermined pressure is vented from the base end side to the main pipe while the drain valve is closed, and is diffused from the air outlet through the branch pipe. At this time, since each air jet is located in the upper part of the branch pipe, most of the air diffused by the buoyancy of the air due to the density difference from the mixed liquid before reaching the end opening is jetted from the air jet.
[0010]
Since the air outlet has a small diameter, the air bubbles to be ejected have a small diameter, and the oxygen dissolution efficiency is increased, so that the blower or the like of the air source can be downsized to reduce power consumption. In addition, by reducing the diameter of the air jets, the number of air jets arranged per unit area can be increased, which increases the degree of dispersion of the air jets, so that the aerated air is uniformly diffused. This increases the cleaning effect.
[0011]
Even if the air outlet is suddenly blocked by foreign matter, low-fluid sludge, large flocs, etc., the air is blown out from the end opening of the branch pipe to ensure a predetermined amount of aeration air. Cleaning can be continued and sludge blockage between the membranes can be prevented from occurring due to insufficient cleaning of the membrane surface until the next regular cleaning.
[0012]
At the time of cleaning, the drain valve is opened in a state where air of a predetermined pressure is supplied from the air source to the main pipe, and the air supplied to the main pipe is exhausted from the exhaust port to atmospheric pressure or a predetermined depth of water through the diffused drain pipe.
[0013]
At this time, the exhaust opening opens to the upper position of the trunk pipe, and the end opening opening and the air outlet of the branch pipe open to the lower position of the trunk pipe, so that the air outlet and the end opening of the branch pipe Due to the pressure difference with the main pipe, the liquid in the tank flows back into the branch pipe and the main pipe through the end opening of the branch pipe and the air outlet, and the in-tank liquid enters the diffused drain pipe together with the air. It is discharged from the exhaust port.
[0014]
The liquid in the tank in the main pipe acts as a resistance that hinders air flow, and the air flow pulsates, and the pressure in the main pipe repeatedly changes suddenly. The air and the liquid in the tank are intermittently discharged from the tank, and the liquid in the tank intermittently flows into the main pipe through the branch pipe.
[0015]
The rapid inflow of the liquid in the tank through this branch pipe is repeatedly generated, so that the sludge adhering to the inside of the branch pipe is effectively washed. Sludge adhering to the inside of the branch pipe is dried by the air at the time of air diffusion, but the liquid in the tank infiltrates the sludge to promote the separation of the sludge. At the same time, it is discharged from the exhaust port.
[0016]
Therefore, by simply opening the drain valve, the inside of the branch pipe, the air outlet, the end opening, and the inside of the trunk pipe can be cleaned, preventing obstruction of the diffuser pipe by dry sludge. Therefore, it is possible to reduce the diameter of the air outlet of the branch pipe that is easily clogged with the drying sludge.
[0017]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings. In FIG. 1 to FIG. 4, an aeration device 2 and a membrane separation device 3 disposed above the aeration device 2 are immersed in the aeration tank 1. The membrane separation device 3 is not essential for the aeration tank 1, but is used as a solid-liquid separation means for activated sludge in the membrane separation activated sludge method according to the present embodiment.
[0018]
The membrane separation device 3 can use various types of separation membranes, for example, 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.
[0019]
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.
[0020]
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, communicates with the trunk pipe 6 at one upper end, has open ports 10a at both ends located below the trunk pipe 6, and has a smaller diameter than the end open port 10a on the upper surface. A plurality of air jets 10b are provided.
[0021]
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. The diffuser case 4 is fixed to the bottom of the tank, and the membrane separation device 3 can be moved up and down along a guide 13 provided between the diffuser case 4 and the tank opening.
[0022]
Hereinafter, the operation of the above-described configuration will be described. During the normal aeration operation, the drain valve 12 is in a closed state, and the air supplied from the blower 8 passes through the trunk pipe 6 from the air outlet 10b of each branch pipe 7 into the mixed liquid in the aeration tank 1. To erupt. At this time, since each air jet 10b is located in the upper part of the branch pipe 7, most of the air diffused by the buoyancy of the air due to the density difference from the mixed liquid until reaching the end opening 10a is from the air jet 10b. Erupts.
[0023]
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. In this air diffused state, since the air outlet 10b has a small diameter, the air bubbles to be ejected have a small diameter, and the oxygen dissolution efficiency is increased, so that the blower 8 of the air source can be reduced in size and the power consumption can be reduced. Further, by reducing the diameter of the air outlet 10b, it is possible to increase the number of air outlets 10b arranged per unit area, thereby increasing the dispersity of the air outlet 10b, so that the aerated air is uniform. Aeration effect is enhanced by aeration.
[0024]
Even if the air outlet 10b is suddenly blocked by foreign matter, sludge with low fluidity, large flocs, etc., a predetermined amount of aerated air is secured by the air jetting from the end opening 10a of the branch pipe 7. Thus, the membrane surface cleaning can be continued, and the sludge blockage between the membranes can be prevented from occurring due to the lack of the membrane surface cleaning until the next regular cleaning.
[0025]
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.
[0026]
At this time, the exhaust port 11 opens under atmospheric pressure at a position above the trunk pipe 6, and the opening 10a and the air outlet 10b open at a position below the trunk pipe 6 to open as shown in FIG. Due to the pressure difference between the pressure P0 acting on the port 10a and the pressure P1 acting on the main pipe 6, the mixed liquid in the tank flows back into the branch pipe 7 and the main pipe 6 through the open port 10a and the air outlet 10b. To do.
[0027]
The mixed liquid in the tank that has flowed in reverse is washed out with sludge adhering to the inside of the branch pipe 7 and washed with water, and is discharged from the exhaust port 11 through the diffused drain pipe 9 together with the air flowing through the trunk pipe 6. Although the sludge adhering to the inside of the branch pipe 7 is dried by the air at the time of air diffusion, peeling of the sludge is promoted by infiltration of the mixed liquid in the tank into the sludge.
[0028]
The mixed liquid in the tank that has flowed into the main pipe 6 acts as a resistance that inhibits the ventilation of air, and the air flow pulsates. In particular, the pressure in the trunk pipe 6 increases because the liquid mixture in the tank staying in the vertical portion of the diffuser drain pipe 9 inhibits the exhaust, and the liquid mixture in the tank staying due to the increase in pressure is discharged all at once. The pressure drops.
[0029]
In this way, the internal pressure of the trunk pipe 6 is repeatedly changed suddenly, whereby air and the mixed liquid in the tank are alternately and intermittently discharged from the exhaust port 11 of the diffuser drain pipe 9, and the branches The mixed liquid in the tank intermittently flows into the main pipe 6 through the pipe 7. The rapid inflow of the mixed liquid in the tank to the branch pipe 7 is repeatedly generated, so that manual operation and repeated operation by a control device are not performed, and the branch pipe 7 is provided inside, the open port 10a, and the air jet port 10b. The adhering sludge can be repeatedly washed with water to effectively remove the sludge.
[0030]
【The invention's effect】
As described above, according to the present invention, the inside of the branch pipe, the end opening, the air outlet, and the main pipe can be cleaned by a simple operation by simply opening the drain valve. It becomes possible to reduce the diameter of the air outlet of the branch pipe that is easily blocked by the dry sludge by preventing the air diffuser from being blocked. By reducing the diameter of the air outlet, air bubbles become smaller and the oxygen dissolution efficiency increases, so the power source can be reduced by reducing the size of the air source blower, etc. It is possible to increase the number of air outlets arranged in the air outlet to increase the degree of dispersion of the air outlets, and to uniformly diffuse the aerated air to enhance the cleaning effect. Even if the air outlet suddenly closes due to large floc sludge, etc., the air can be ejected from the end opening of the branch pipe, so that a predetermined amount of aeration air can be secured and membrane cleaning can be continued. It is possible to prevent sludge clogging between the membranes due to insufficient membrane surface cleaning until the next regular cleaning.
[Brief description of the drawings]
FIG. 1 is a front view showing an air diffuser according to an embodiment of the present invention.
FIG. 2 is a perspective view of the air diffuser.
FIG. 3 is a cross-sectional view of a main part of the air diffuser.
FIG. 4 is an enlarged view of a main part of the air diffuser.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Aeration tank 2 Air diffuser 3 Membrane separator 4 Air diffuser case 5 Air diffuser pipe 6 Trunk pipe 7 Branch pipe 8 Blower 9 Air diffuser drain pipe 10a Opening port 10b Air outlet 11 Exhaust port 12 Drain valve 13 Guide

Claims (1)

槽内に浸漬して水平方向に配置し、基端側が空気供給源に連通する幹配管と、幹配管に連通するとともに、先端が幹配管の下方位置で開口する複数の枝配管と、一端が幹配管の先端側に連通するとともに、他端が幹配管の上方位置で排気口として開口する散気ドレン管と、散気ドレン管に設けたドレンバルブとを有し、各枝配管は端部に開放口を有し、上面に端部開放口より小口径の複数の空気噴出口を設けたことを特徴とする散気装置。Immerse in the tank and place in the horizontal direction, the trunk pipe whose base end side communicates with the air supply source, a plurality of branch pipes that communicate with the trunk pipe, and whose tip opens at a position below the trunk pipe, and one end It has a diffused drain pipe that communicates with the leading end side of the trunk pipe and the other end opens as an exhaust port at an upper position of the trunk pipe, and a drain valve provided in the diffused drain pipe. Each branch pipe has an end portion. An air diffuser characterized in that the air diffuser has a plurality of air outlets having an opening on the upper surface and a smaller diameter than the end opening.
JP2000389658A 2000-12-04 2000-12-22 Air diffuser Expired - Lifetime JP3784252B2 (en)

Priority Applications (18)

Application Number Priority Date Filing Date Title
JP2000389658A JP3784252B2 (en) 2000-12-22 2000-12-22 Air diffuser
AU24103/02A AU783464B2 (en) 2000-12-04 2001-11-26 Air diffuser and flushing method thereof
US10/182,564 US6843470B2 (en) 2000-12-04 2001-11-26 Air diffuser and flushing method thereof
CNB018045073A CN1204961C (en) 2000-12-04 2001-11-26 Air diffuser and flushing method thereof
DE2001625594 DE60125594T2 (en) 2000-12-04 2001-11-26 AIR DISTRIBUTION AND SPILLING PROCESS THEREFOR
EP01999424A EP1358005B1 (en) 2000-12-04 2001-11-26 Air diffuser and flushing method thereof
ES01999424T ES2282329T3 (en) 2000-12-04 2001-11-26 AIR DIFFUSER AND CLEANING METHOD OF THE SAME.
KR1020027010060A KR100768873B1 (en) 2000-12-04 2001-11-26 Air diffuser and flushing method thereof
PCT/JP2001/010297 WO2002045833A1 (en) 2000-12-04 2001-11-26 Air diffuser and flushing method thereof
CA 2398460 CA2398460C (en) 2000-12-04 2001-11-26 Air diffuser and flushing method thereof
AT01999424T ATE349271T1 (en) 2000-12-04 2001-11-26 AIR DISTRIBUTOR AND FLUSHING METHOD THEREOF
CA 2398461 CA2398461C (en) 2000-12-04 2001-11-30 Multistage immersion type membrane separator and high-concentration wastewater treatment facility using same
AU18521/02A AU781443B2 (en) 2000-12-04 2001-11-30 Multistage immersion type membrane separator and high-concentration wastewater treatment facility using same
EP20010999419 EP1341597A1 (en) 2000-12-04 2001-11-30 Multistage immersion type membrane separator and high-concentration wastewater treatment facility using same
US10/182,636 US6843908B2 (en) 2000-12-04 2001-11-30 Multistage immersion type membrane separator and high-concentration wastewater treatment facility using same
CNB018044522A CN1241676C (en) 2000-12-04 2001-11-30 Multistage immersion type membrane separator and high-conentration wastewater treatment facility using same
KR20027010016A KR100768841B1 (en) 2000-12-04 2001-11-30 Multistage immersion type membrane separator and high-concentration wastewater treatment facility using same
PCT/JP2001/010524 WO2002045827A1 (en) 2000-12-04 2001-11-30 Multistage immersion type membrane separator and high-concentration wastewater treatment facility using same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000389658A JP3784252B2 (en) 2000-12-22 2000-12-22 Air diffuser

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JP2002186991A JP2002186991A (en) 2002-07-02
JP3784252B2 true JP3784252B2 (en) 2006-06-07

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104870377B (en) * 2012-10-19 2018-03-13 三菱化学株式会社 Air diffusion apparatus, dissipate gas method and water treatment facilities
JP6308062B2 (en) * 2013-09-26 2018-04-11 三菱ケミカル株式会社 Air diffuser and water treatment device
CN113429097B (en) * 2021-08-11 2024-05-14 怡灏环境技术有限公司 Sludge fermentation equipment

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