JP3290577B2 - Immersion type membrane separation device - Google Patents

Immersion type membrane separation device

Info

Publication number
JP3290577B2
JP3290577B2 JP30183795A JP30183795A JP3290577B2 JP 3290577 B2 JP3290577 B2 JP 3290577B2 JP 30183795 A JP30183795 A JP 30183795A JP 30183795 A JP30183795 A JP 30183795A JP 3290577 B2 JP3290577 B2 JP 3290577B2
Authority
JP
Japan
Prior art keywords
case
membrane
separation device
membrane separation
water
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
Application number
JP30183795A
Other languages
Japanese (ja)
Other versions
JPH09141066A (en
Inventor
山田  豊
清司 和泉
謙治 久保田
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
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Filing date
Publication date
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Priority to JP30183795A priority Critical patent/JP3290577B2/en
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Classifications

    • 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

Landscapes

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

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、処理槽の内部に設
置される浸漬型膜分離装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a submerged membrane separation apparatus installed inside a processing tank.

【0002】[0002]

【従来の技術】たとえば、し尿等の有機性排水を処理す
る水処理設備においては、図2および図3に示したよう
に、処理槽1の内部に、被処理水2を膜分離する浸漬型
膜分離装置3を設置している。
2. Description of the Related Art For example, in a water treatment facility for treating organic wastewater such as night soil, as shown in FIGS. 2 and 3, an immersion type for separating water to be treated 2 into a membrane in a treatment tank 1 is shown. A membrane separation device 3 is provided.

【0003】膜分離装置3は、上下が開口した箱状の膜
ケース4の内部に上下方向に配置する平板状の膜カート
リッジ5を一定間隔で並列に配置し、同じく上下が開口
した箱状の散気ケース6の内部に、槽外のブロワ7など
の空気供給源に連通した散気装置8を配置し、膜ケース
4と散気ケース6とを互いに上下に配置することにより
構成されている。膜ケース4や膜カートリッジ5や散気
ケース6の大きさ等は、被処理水の性状・流入量や設置
スペースを考慮して決定されるが、たとえば、膜ケース
4の高さ1m、散気ケース6の高さ1.5m、膜カート
リッジ5の間隔5〜10mmとされる。
[0003] The membrane separation device 3 is configured such that flat membrane cartridges 5 arranged vertically in a box-shaped membrane case 4 having an open top and bottom are arranged in parallel at regular intervals, and a box-like membrane having an open top and bottom. A diffuser 8 communicating with an air supply source such as a blower 7 outside the tank is disposed inside the diffuser case 6, and the membrane case 4 and the diffuser case 6 are arranged above and below each other. . The size and the like of the membrane case 4, the membrane cartridge 5, and the air diffuser case 6 are determined in consideration of the properties and the inflow amount of the water to be treated and the installation space. The height of the case 6 is 1.5 m, and the distance between the membrane cartridges 5 is 5 to 10 mm.

【0004】膜カートリッジ5は、濾板9の両表面に有
機濾過膜10を配置し、濾板9と濾過膜10との間に連
通する透過水流路(図示せず)を濾板9に形成し、透過
水流路に連通する吸引チューブ11と集水管12を設け
ることにより構成されている。そして、集水管12に連
通するように、透過水管13や吸引ポンプ14などの吸
引手段が設けられる。
[0004] In the membrane cartridge 5, an organic filtration membrane 10 is arranged on both surfaces of a filter plate 9, and a permeated water channel (not shown) communicating between the filter plate 9 and the filtration membrane 10 is formed in the filter plate 9. The suction tube 11 and the water collection tube 12 communicating with the permeated water flow path are provided. Then, suction means such as a permeated water pipe 13 and a suction pump 14 are provided so as to communicate with the water collection pipe 12.

【0005】このような構成において、膜分離装置3に
より被処理水2を膜分離する際には、吸引ポンプ14に
よって透過水管13,集水管12,吸引チューブ11を
通じて膜カートリッジ5の透過水流路に吸引圧を負荷す
ることにより、あるいは膜カートリッジ5より上方の被
処理水2の水頭を濾過駆動圧とすることにより、被処理
水2中に含まれる活性汚泥などの懸濁物質を濾過膜10
で捕捉し、濾過膜10を透過して透過水流路内に流入し
た透過水を吸引チューブ11,集水管12,透過水管1
3を通じて処理槽1の外部へ取り出している。
In such a configuration, when the water to be treated 2 is subjected to membrane separation by the membrane separation device 3, the suction pump 14 passes through the permeated water pipe 13, the water collection pipe 12, and the suction tube 11 to the permeated water flow path of the membrane cartridge 5. By applying suction pressure or by setting the head of the water 2 to be treated above the membrane cartridge 5 to a filtration drive pressure, suspended substances such as activated sludge contained in the water to be treated 2 can be removed from the filtration membrane 10.
The permeated water permeated through the filtration membrane 10 and flowed into the permeated water flow path through the filtration membrane 10 is sucked by the suction tube 11, the water collection tube 12,
3 to the outside of the processing tank 1.

【0006】このとき、ブロワ7より供給する空気を散
気装置8の散気孔8aを通じて散気し、散気した空気の
気泡およびそれにより生起される上昇水流を膜カートリ
ッジ5,5間の間隙に流入させることによって、気泡と
上昇水流とにより膜カートリッジ5の膜面全体を均一に
洗浄し、上昇水流により、膜面における濃度分極を小さ
くして濾過抵抗を小さくするとともに、槽内を旋回する
攪拌流を形成するようにしている。
At this time, the air supplied from the blower 7 is diffused through the air diffusing holes 8a of the diffusing device 8, and the air bubbles of the diffused air and the rising water flow generated thereby are introduced into the gap between the membrane cartridges 5, 5. By inflowing, the entire membrane surface of the membrane cartridge 5 is uniformly washed by the bubbles and the rising water flow, and the rising water flow reduces the concentration polarization on the membrane surface to reduce the filtration resistance and stirs in the tank. To create a flow.

【0007】[0007]

【発明が解決しようとする課題】上記したようにして膜
カートリッジ5の膜面洗浄を気泡と上昇水流とにより行
う際には、洗浄効果を高めるために、散気する空気量を
多くすることが考えられるが、膜カートリッジ5,5間
の間隙に流入する気泡量が多すぎると、逆にこの間隙へ
の被処理液の流入量が少なくなり、処理量が低下するの
で好ましくない。
When the cleaning of the membrane surface of the membrane cartridge 5 is performed by using air bubbles and a rising water flow as described above, it is necessary to increase the amount of diffused air in order to enhance the cleaning effect. It is conceivable that if the amount of bubbles flowing into the gap between the membrane cartridges 5 and 5 is too large, on the contrary, the flow rate of the liquid to be treated into this gap decreases, and the processing amount decreases.

【0008】そこで、上昇水流の流速を大きくすること
が考えられるが、上記した従来の装置では、散気ケース
内で散気される空気の気泡によってのみ上昇水流を生起
しているので、容易に上昇流速の増大を図れない。
Therefore, it is conceivable to increase the flow velocity of the rising water flow. However, in the above-described conventional apparatus, the rising water flow is generated only by air bubbles diffused in the diffusion case. The ascending flow velocity cannot be increased.

【0009】本発明は上記課題を解決するもので、少な
い空気量によっても上昇水流の流速を大きくすることが
でき、効率的に膜面洗浄できる浸漬型膜分離装置を提供
することを目的とするものである。
An object of the present invention is to solve the above-mentioned problems, and an object of the present invention is to provide an immersion type membrane separation apparatus which can increase the flow velocity of the rising water flow even with a small amount of air and can efficiently clean the membrane surface. Things.

【0010】[0010]

【課題を解決するための手段】上記問題を解決するため
に、本発明の浸漬型膜分離装置は、処理槽内の被処理水
に浸漬して上下が開口した箱状のケースを設け、ケース
内の上部に、上下方向に配置する膜カートリッジを一定
間隔で並行に設け、ケース内の膜カートリッジの下方に
散気装置を設けて、散気装置より散気される空気の気泡
とそのエアリフト作用により生起される上昇水流とによ
り膜カートリッジの膜面を洗浄するように構成した浸漬
型膜分離装置において、前記ケースの上部に、ケースを
抜け出た気泡および上昇水流を上方に導く箱枠状の整流
ケースを処理槽の内壁から離間して設けたものである。
Means for Solving the Problems To solve the above problems, the immersion type membrane separation apparatus of the present invention is provided with a box-shaped case which is immersed in water to be treated in a treatment tank and has an open top and bottom. In the upper part of the inside, membrane cartridges arranged vertically are provided in parallel at a fixed interval, and an air diffuser is provided below the membrane cartridge in the case, air bubbles diffused from the air diffuser and its air lift action In the immersion type membrane separation device configured to wash the membrane surface of the membrane cartridge with the rising water flow generated by the above, a box frame-shaped rectifier that guides upwardly the bubbles and the rising water flow that have escaped from the case to the upper part of the case. The case is provided separately from the inner wall of the processing tank .

【0011】また本発明の浸漬型膜分離装置は、整流ケ
ースを、その上端部が水面下約30cmに位置するよう
に設けたものである。また本発明の浸漬型膜分離装置
は、整流ケースを、少なくとも一側面を脱着自に形成し
たものである。
Further, in the immersion type membrane separation device of the present invention, the rectifying case is provided such that the upper end thereof is located about 30 cm below the water surface. Further, in the immersion type membrane separation device of the present invention, at least one side surface of the rectifying case is detachably formed.

【0012】上記した構成によれば、ケース内の下部に
おいて、散気装置より散気される空気の気泡のエアリフ
ト作用によって上昇水流が生起され、この上昇水流と気
泡とが、膜カートリッジ間の間隙を通過し、ケースを抜
け出た後には、整流ケースの内部に流入して左右方向に
拡散することなく上方に導かれる。そして、整流ケース
の内部においても、気泡のエアリフト作用により上昇水
流が生起され、整流ケース内に流入した上昇水流の流速
は高められる。このようにして、ケースを抜け出た上昇
水流の流速が整流ケースにおいてさらに増大される結
果、ケース内の上昇水流の流速も高くなり、膜面洗浄効
果が増大する。
[0012] According to the above-described structure, an ascending water flow is generated in the lower portion of the case by the air-lifting action of the air bubbles diffused by the air diffuser, and the ascending water flow and the air bubbles are generated in the gap between the membrane cartridges. After passing through the case and exiting the case, it flows into the rectifying case and is guided upward without diffusing in the left-right direction. Then, also inside the rectifying case, a rising water flow is generated by the air lift action of the bubbles, and the flow velocity of the rising water flow flowing into the rectifying case is increased. In this way, as a result of the flow velocity of the rising water flowing out of the case being further increased in the rectifying case, the flow velocity of the rising water flowing in the case is also increased, and the membrane surface cleaning effect is increased.

【0013】整流ケースは上下方向に長いほどエアリフ
ト作用による流速増大効果が高くなるが、水面付近まで
整流ケースを設けると内部を上昇した水流が水面上に盛
り上がって、スムーズな槽内旋回流が生じにくくなる。
しかるに、上記したような、整流ケースの上端部が水面
下約30cmに位置した構成によれば、整流ケースの上
端部に達した上昇水流は速やかに水面と平行な流れに転
じるので、処理槽内にスムーズな旋回流が形成される。
The longer the flow straightening case is in the vertical direction, the greater the effect of increasing the flow velocity by the air lift action. However, if the flow straightening case is provided near the water surface, the water flow rising inside rises above the water surface, and a smooth swirling flow in the tank is generated. It becomes difficult.
However, according to the above-described configuration in which the upper end of the rectifying case is located at about 30 cm below the water surface, the rising water flow that has reached the upper end of the rectifying case quickly turns into a flow parallel to the water surface. A smooth swirling flow is formed.

【0014】エアリフトケースの少なくとも一側面を脱
着自在に形成した構成によれば、膜間閉塞が生じたとき
などは、脱着自在な側面を取り外して容易に作業でき
る。
According to the structure in which at least one side surface of the air lift case is detachably formed, the work can be easily performed by removing the detachable side surface when an inter-membrane blockage occurs.

【0015】[0015]

【発明の実施の形態】以下、本発明の実施の形態を図面
を参照しながら説明する。図1において、処理槽1内の
被処理水2に浸漬して設けた浸漬型膜分離装置3は、図
2および図3を用いて説明した従来のものとほぼ同様に
構成されており、上下が開口した箱状の膜ケース4と散
気ケース6とを互いに上下に配置し、膜ケース4の内部
に、上下方向に配置する膜カートリッジ5を適当間隔で
並行に設け、散気ケース6の内部に散気装置8を設けて
いる。
Embodiments of the present invention will be described below with reference to the drawings. In FIG. 1, an immersion type membrane separation device 3 provided by being immersed in water to be treated 2 in a treatment tank 1 is configured substantially in the same manner as the conventional one described with reference to FIGS. A box-shaped membrane case 4 and an air diffuser case 6 each having an opening are arranged vertically above and below, and membrane cartridges 5 arranged vertically in the membrane case 4 are provided in parallel at appropriate intervals. An air diffuser 8 is provided inside.

【0016】ここで、浸漬型膜分離装置3が従来のもの
と異なるのは、膜ケース4の上部に、膜ケース4を抜け
出た気泡および上昇水流を上方に導く箱枠状の整流ケー
ス15を設けた点である。
Here, the immersion type membrane separation device 3 is different from the conventional one in that a box frame-shaped rectifying case 15 for guiding bubbles and rising water flowing out of the membrane case 4 to the upper portion of the membrane case 4 is provided. This is the point provided.

【0017】整流ケース15は、上端部15aが水面下
約30cmに位置する高さに形成されるとともに、隣接
する側面15b,15cが脱着自在に形成されている。
以下、上記構成における作用を説明する。
The rectifying case 15 has an upper end 15a formed at a height of about 30 cm below the water surface, and has adjoining side surfaces 15b and 15c detachably formed.
Hereinafter, the operation of the above configuration will be described.

【0018】吸引ポンプ14を駆動して、膜分離装置3
の膜カートリッジ5により被処理水2を膜分離し、活性
汚泥などの懸濁物質を処理槽1内に残留させ、透過水を
吸引チューブ11,集水管12,透過水管13を通じて
処理槽1の外部へ取り出す。
By driving the suction pump 14, the membrane separation device 3
The water to be treated 2 is subjected to membrane separation by the membrane cartridge 5, and suspended substances such as activated sludge remain in the treatment tank 1, and the permeated water is passed through the suction tube 11, the water collecting pipe 12 and the permeated water pipe 13 to the outside of the treatment tank 1. To take out.

【0019】同時に、ブロワ7により空気を供給して散
気装置8を通じて散気し、散気した空気の気泡およびそ
れにより生起される上昇水流を膜カートリッジ5,5間
の間隙に流入させ、それによって、気泡と上昇水流とに
より膜カートリッジ5の膜面を洗浄し、上昇水流によ
り、膜面における濃度分極を小さくして濾過抵抗を小さ
くする。
At the same time, air is supplied by the blower 7 and diffused through the diffuser 8, and the air bubbles of the diffused air and the rising water flow generated thereby are caused to flow into the gap between the membrane cartridges 5, 5. As a result, the membrane surface of the membrane cartridge 5 is washed with the bubbles and the rising water flow, and the concentration polarization on the membrane surface is reduced by the rising water flow to reduce the filtration resistance.

【0020】このとき、膜カートリッジ5,5間の間隙
を通過した上昇水流と気泡とは、膜ケース4を抜け出た
後に整流ケース15の内部に流入するが、整流ケース1
5によって拡散することなく上方に導かれ、上昇水流
は、整流ケース15の内部で、上昇するほど膨張して速
度が大きくなっている気泡のエアリフト作用を受けて流
速が増大する。このようにして膜ケース4の上方におい
て上昇水流の流速が増大する結果、膜ケース4内の上昇
水流の流速も高まり、膜カートリッジ5の膜面洗浄効果
が高くなる。これにより、処理量が増大するとともに、
膜カートリッジ5の逆洗や薬洗の頻度低減が可能にな
る。
At this time, the rising water flow and the bubbles that have passed through the gap between the membrane cartridges 5 and 5 flow out of the membrane case 4 and flow into the rectification case 15.
The rising water flow is guided upward without being diffused by 5, and the rising water flow is subjected to the airlift effect of the bubbles, which expand and increase in speed as rising, inside the rectifying case 15, and the flow velocity increases. As a result, the flow rate of the rising water flow increases above the membrane case 4, so that the flow rate of the rising water flow inside the membrane case 4 also increases, and the membrane surface cleaning effect of the membrane cartridge 5 increases. This increases the amount of processing and
The frequency of back washing and chemical washing of the membrane cartridge 5 can be reduced.

【0021】整流ケース15の上端部に達した上昇水流
は、整流ケース15の上端部15aが水面下約30cm
に位置していることにより、速やかに水面と平行な流れ
に転じ、その後、整流ケース15の外周面に沿って散気
ケース6の下部に向かう下降流に転じる。したがって、
上昇水流が水面上に盛り上がるときのような抵抗を生じ
ることなく、槽内全体をスムーズに旋回する攪拌流が形
成される。
The rising water flow that has reached the upper end of the rectifying case 15 is such that the upper end 15a of the rectifying case 15 is about 30 cm below the water surface.
, The flow quickly changes to a flow parallel to the water surface, and then changes to a downward flow along the outer peripheral surface of the rectifying case 15 toward the lower part of the air diffuser case 6. Therefore,
The agitated flow that smoothly swirls the entire inside of the tank is formed without generating the resistance that occurs when the rising water flow rises above the water surface.

【0022】膜カートリッジ5,5間の間隙に閉塞が生
じたときなどは、脱着自在な側面15b,15cを取り
外して作業を行う。
When the gap between the membrane cartridges 5 and 5 is closed, the work is performed by removing the detachable side surfaces 15b and 15c.

【0023】[0023]

【発明の効果】以上のように本発明によれば、複数枚の
膜カートリッジと散気装置とを互いに上下に収容したケ
ースの上部に箱枠状の整流ケースを設けて、ケースを抜
け出た気泡および上昇水流を拡散させることなく上方に
導くようにしたことにより、従来と同等の空気量によっ
て、膜カートリッジ間を流れる上昇水流の流速を高める
ことができる。この結果、膜カートリッジの膜面の汚染
を低減できるので、膜カートリッジの運転サイクルを長
くすることができ、処理量が増大するとともに、逆洗や
薬洗などの洗浄頻度を低減できるためメンテナンスが容
易になる。また、従来より少ない空気量によっても、ケ
ース内の上昇水流の流速を従来と同等またはより大きく
できるので、省エネルギーを図れる。
As described above, according to the present invention, a box frame-shaped rectifying case is provided above a case in which a plurality of membrane cartridges and an air diffuser are housed one above the other, and air bubbles that escape from the case are provided. In addition, since the rising water flow is guided upward without being diffused, the flow rate of the rising water flowing between the membrane cartridges can be increased with the same amount of air as in the related art. As a result, the contamination of the membrane surface of the membrane cartridge can be reduced, so that the operation cycle of the membrane cartridge can be lengthened, the processing amount can be increased, and the frequency of cleaning such as back washing and chemical washing can be reduced, so that maintenance is easy. become. Also, the flow rate of the rising water flow in the case can be made equal to or greater than that of the conventional case even with a smaller amount of air than in the conventional case, so that energy can be saved.

【0024】また、整流ケースの上端部を水面下約30
cmに位置させるようにしたことにより、整流ケースの
上端部に達した上昇水流を速やかに水面と平行な流れに
転じさせることができ、槽内を水面近くから底部まで全
体にわたってスムーズに旋回する攪拌流を形成できる。
よって、活性汚泥を含んだ被処理水などの場合も、槽内
局部での汚泥等の堆積・腐敗などを防止できる。
Further, the upper end of the rectifying case is set at about 30
cm, the rising water flow that has reached the upper end of the rectifying case can be quickly turned into a flow parallel to the water surface, and the inside of the tank smoothly swirls from near the water surface to the bottom. A flow can be formed.
Therefore, even in the case of water to be treated containing activated sludge, accumulation and decay of sludge or the like at a local portion in the tank can be prevented.

【0025】また、エアリフトケースの少なくとも一側
面を脱着自在に形成するようにしたことにより、膜間閉
塞が生じたときなどのメンテナンスを容易に行える。
Further, since at least one side surface of the air lift case is formed so as to be detachable, maintenance can be easily performed in the case where an inter-membrane blockage occurs.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の一実施形態の浸漬型膜分離装置を設置
した処理槽の全体構成を示した説明図である。
FIG. 1 is an explanatory diagram showing an overall configuration of a processing tank provided with a submerged membrane separation device according to an embodiment of the present invention.

【図2】従来の浸漬型膜分離装置を設置した処理槽の全
体構成を示した説明図である。
FIG. 2 is an explanatory diagram showing an overall configuration of a processing tank provided with a conventional immersion type membrane separation device.

【図3】図2に示した浸漬型膜分離装置の構成を示した
説明図である。
FIG. 3 is an explanatory diagram showing a configuration of the immersion type membrane separation device shown in FIG.

【符号の説明】[Explanation of symbols]

1 処理槽 2 被処理水 3 浸漬型膜分離装置 4 膜ケース 5 膜カートリッジ 6 散気ケース 8 散気装置 15 整流ケース 15a 整流ケースの上端部 15b,15c 整流ケースの側面 DESCRIPTION OF SYMBOLS 1 Treatment tank 2 Treated water 3 Immersion type membrane separation device 4 Membrane case 5 Membrane cartridge 6 Air diffuser case 8 Air diffuser 15 Rectifier case 15a Upper end of rectifier case 15b, 15c Side of rectifier case

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平9−75938(JP,A) 特開 平8−299979(JP,A) 特開 平8−299984(JP,A) 特開 平8−332358(JP,A) 特開 平7−39873(JP,A) (58)調査した分野(Int.Cl.7,DB名) B01D 63/08 B01D 65/02 520 C02F 1/44 ZAB ────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-9-75938 (JP, A) JP-A-8-299979 (JP, A) JP-A-8-299984 (JP, A) JP-A-8-99984 332358 (JP, A) JP-A-7-39873 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) B01D 63/08 B01D 65/02 520 C02F 1/44 ZAB

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 処理槽内の被処理水に浸漬して上下が開
口した箱状のケースを設け、ケース内の上部に、上下方
向に配置する膜カートリッジを一定間隔で並行に設け、
ケース内の膜カートリッジの下方に散気装置を設けて、
散気装置より散気される空気の気泡とそのエアリフト作
用により生起される上昇水流とにより膜カートリッジの
膜面を洗浄するように構成した浸漬型膜分離装置におい
て、前記ケースの上部に、ケースを抜け出た気泡および
上昇水流を上方に導く箱枠状の整流ケースを処理槽の内
壁から離間して設けたことを特徴とする浸漬型膜分離装
置。
1. A box-shaped case which is immersed in water to be treated in a treatment tank and has an open top and bottom is provided, and upper and lower membrane cartridges arranged in a vertical direction are provided in parallel at a predetermined interval.
A diffuser is provided below the membrane cartridge in the case ,
In the immersion type membrane separation device configured to wash the membrane surface of the membrane cartridge by air bubbles diffused by the air diffuser and the rising water flow generated by the air lift action, a case is provided above the case. A box-shaped rectifying case that guides the escaped air bubbles and rising water flow upwards inside the treatment tank
An immersion-type membrane separation device provided apart from a wall .
【請求項2】 整流ケースを、その上端部が水面下約3
0cmに位置するように設けたことを特徴とする請求項
1記載の浸漬型膜分離装置。
2. A rectifying case, the upper end of which is about 3 inches below the surface of the water.
2. The immersion type membrane separation device according to claim 1, wherein the immersion type membrane separation device is provided so as to be located at 0 cm.
【請求項3】 整流ケースを、少なくとも一側面を脱着
自在に形成したことを特徴とする請求項1または請求項
2のいずれかに記載の浸漬型膜分離装置。
3. The immersion type membrane separation device according to claim 1, wherein at least one side surface of the rectification case is detachably formed.
JP30183795A 1995-11-21 1995-11-21 Immersion type membrane separation device Expired - Lifetime JP3290577B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30183795A JP3290577B2 (en) 1995-11-21 1995-11-21 Immersion type membrane separation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30183795A JP3290577B2 (en) 1995-11-21 1995-11-21 Immersion type membrane separation device

Publications (2)

Publication Number Publication Date
JPH09141066A JPH09141066A (en) 1997-06-03
JP3290577B2 true JP3290577B2 (en) 2002-06-10

Family

ID=17901760

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30183795A Expired - Lifetime JP3290577B2 (en) 1995-11-21 1995-11-21 Immersion type membrane separation device

Country Status (1)

Country Link
JP (1) JP3290577B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007122839A1 (en) 2006-03-27 2007-11-01 Toray Industries, Inc. Membrane element, membrane unit and multistage membrane unit

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GB9914854D0 (en) * 1999-06-25 1999-08-25 Wilkes Ian P Self cleaning membrane device for filtration used in submerged operation
CN1116097C (en) * 1999-08-18 2003-07-30 中国科学院生态环境研究中心 Superfilter membrane type separator
JP3479632B2 (en) * 2000-06-26 2003-12-15 青木電器工業株式会社 Wastewater treatment equipment
JP2003093849A (en) * 2001-09-27 2003-04-02 Yuasa Corp Immersion type membrane filter device
JP3732488B2 (en) * 2003-06-20 2006-01-05 青木電器工業株式会社 Wastewater treatment equipment
JP4748784B2 (en) * 2005-09-26 2011-08-17 株式会社野生水族繁殖センター Air pumping equipment
JP5283696B2 (en) * 2008-05-30 2013-09-04 株式会社クボタ Immersion membrane separator
JP2012161791A (en) * 2011-01-20 2012-08-30 Kubota Corp Membrane separation equipment, membrane separation device and method for operating membrane separation equipment
CN106984197A (en) * 2017-05-27 2017-07-28 湖南科技大学 A kind of submerged modular construction flat ceramic membrane filtration system
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Publication number Priority date Publication date Assignee Title
JP2930839B2 (en) * 1993-08-02 1999-08-09 株式会社クボタ Water treatment equipment
JP3282445B2 (en) * 1995-04-28 2002-05-13 栗田工業株式会社 Biological treatment equipment
JPH08299984A (en) * 1995-05-02 1996-11-19 Kurita Water Ind Ltd Biological treating device
JPH08332358A (en) * 1995-06-09 1996-12-17 Kubota Corp Membrane separator
JPH0975938A (en) * 1995-09-08 1997-03-25 Kurita Water Ind Ltd Membrane separation device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007122839A1 (en) 2006-03-27 2007-11-01 Toray Industries, Inc. Membrane element, membrane unit and multistage membrane unit

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