JPH0713832Y2 - Membrane module of activated sludge treatment equipment - Google Patents
Membrane module of activated sludge treatment equipmentInfo
- Publication number
- JPH0713832Y2 JPH0713832Y2 JP1989069938U JP6993889U JPH0713832Y2 JP H0713832 Y2 JPH0713832 Y2 JP H0713832Y2 JP 1989069938 U JP1989069938 U JP 1989069938U JP 6993889 U JP6993889 U JP 6993889U JP H0713832 Y2 JPH0713832 Y2 JP H0713832Y2
- Authority
- JP
- Japan
- Prior art keywords
- membrane
- filtration
- membrane module
- activated sludge
- sludge treatment
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Activated Sludge Processes (AREA)
Description
【考案の詳細な説明】 産業上の利用分野 本考案は、有機性廃水の活性汚泥処理装置の膜モジュー
ルに関する。TECHNICAL FIELD The present invention relates to a membrane module of an activated sludge treatment device for organic wastewater.
従来の技術 従来より、有機性廃水の活性汚泥処理装置においては、
たとえば第4図に示すように、曝気槽1内に上下両面が
開放された方形の箱枠2を設け、箱枠2内に複数個の膜
モジュール3を垂直に一定間隔aをおいて配列し、膜モ
ジュール3の下方に散気管4は配置している。5は曝気
槽1に開口する原水供給管、6は曝気槽1の底部に接続
した汚泥引抜きポンプである。膜モジュール3は、凹凸
状に曲成された膜支持体7の両面を濾過膜8により被覆
したもので、膜支持体7の上端部に接続した透過液吸引
管9を介して透過液集水管10に接続されている。透過液
集水管10は、途中に吸引ポンプ11を備え、透過液槽12に
開口している。散気管4は、給気管13を介してブロワー
14に接続されている。Conventional technology Conventionally, in the activated sludge treatment device of organic wastewater,
For example, as shown in FIG. 4, a rectangular box frame 2 whose upper and lower surfaces are open is provided in the aeration tank 1, and a plurality of membrane modules 3 are vertically arranged in the box frame 2 at regular intervals a. The air diffusing tube 4 is arranged below the membrane module 3. Reference numeral 5 is a raw water supply pipe opening to the aeration tank 1, and 6 is a sludge drawing pump connected to the bottom of the aeration tank 1. The membrane module 3 is formed by coating both sides of a membrane support 7 curved in an uneven shape with a filtration membrane 8, and a permeate collection pipe via a permeate suction pipe 9 connected to the upper end of the membrane support 7. Connected to 10. The permeated liquid collecting pipe 10 is provided with a suction pump 11 on the way and opens into a permeated liquid tank 12. The air diffuser 4 is a blower via the air supply pipe 13.
Connected to 14.
原水供給管5から曝気槽1内に供給された原水15は、槽
内で活性汚泥により消化処理されて消化処理水16とな
る。その際、散気管4は、ブロワー14から供給される空
気などの酸素を含有する曝気用気体17を膜モジュール3
の間に吹き込み、活性汚泥中の微生物に酸素を供給す
る。消化処理水16は、膜モジュール3を介して吸引ポン
プ11により吸引され、膜モジュール3により固液分離さ
れる。すなわち、消化処理水16中の汚泥は濾過膜8によ
り捕捉され、他方、濾過膜8を透過した洗浄な透過液18
は、透過液吸引管9から透過液集水管10を経由して透過
液槽12内に貯留される。その際、膜モジュール3の間に
は、曝気用気体17の気泡のエアリフト作用によい消化処
理水16の上昇流が生じており、この上昇流が濾過膜8に
付着した汚泥を濾過膜8から離脱させて、濾過膜8の目
詰りを防止する。The raw water 15 supplied from the raw water supply pipe 5 into the aeration tank 1 is digested by activated sludge in the tank to become digested water 16. At that time, the air diffuser 4 supplies the aeration gas 17 containing oxygen such as air supplied from the blower 14 to the membrane module 3
It is blown in between to supply oxygen to the microorganisms in the activated sludge. The digested water 16 is sucked by the suction pump 11 through the membrane module 3 and is solid-liquid separated by the membrane module 3. That is, the sludge in the digested water 16 is captured by the filtration membrane 8, while the washed permeate 18 that has permeated the filtration membrane 8
Is stored in the permeate tank 12 from the permeate suction pipe 9 through the permeate water collecting pipe 10. At that time, an ascending flow of the digestion-treated water 16 which is good for the air lift action of the bubbles of the aeration gas 17 is generated between the membrane modules 3, and this ascending flow removes the sludge adhering to the filtration film 8 from the filtration film 8. The filter membrane 8 is detached to prevent clogging of the filtration membrane 8.
考案が解決しようとする課題 しかし、上記従来の膜モジュール3においては、吸引状
態のとき、濾過膜8の一部が膜支持体7の凸部に密着し
て両者の間に透過液18の流路がなくなるとともに、その
部分に吸引力が有効に作用しなくなり、濾過機能が低下
する。そのため、濾過膜8の有効濾過面積が減少し、濾
過効率が低下するという問題があった。さらに、膜モジ
ュール3は、構造が複雑で厚さが厚いため、大形にかつ
重くなり、濾過膜8の洗浄・取替えなどのメンテナンス
時に操作が容易でないという問題があった。However, in the above-mentioned conventional membrane module 3, in the suction state, a part of the filtration membrane 8 is brought into close contact with the convex portion of the membrane support 7 and the flow of the permeate 18 between the two is generated. When the passage is eliminated, the suction force does not act effectively on that portion, and the filtration function is deteriorated. Therefore, there is a problem that the effective filtration area of the filtration membrane 8 is reduced and the filtration efficiency is reduced. Further, since the membrane module 3 has a complicated structure and a large thickness, it becomes large and heavy, and there is a problem that it is not easy to operate during maintenance such as cleaning and replacement of the filtration membrane 8.
本考案は、従来の膜モジュールを改良して、このような
問題点を解消することを目的とする。An object of the present invention is to improve the conventional membrane module and eliminate such problems.
課題を解決するための手段 上記目的を達成するために、本考案の活性汚泥処理装置
の膜モジュールは、曝気槽内に浸漬して複数の膜モジュ
ールを垂直に、かつ平行に配置するとともに、隣接する
膜モジュールの相互間に一定の間隙を形成し、膜モジュ
ールの下方に散気手段を設ける活性汚泥処理装置におけ
る膜モジュールであって、中央部に透過液の流路空間を
有する無端の枠体に、枠体の内外を連通する連通孔を設
けて膜支持体を形成し、膜支持体の表裏両面を濾過膜に
より被覆し、膜支持体の表裏両面と濾過膜との間に濾過
膜を透過した透過液の通過可能なスペーサを設け、この
スペーサを剛性を有する格子状ネットで形成した構成と
したものである。Means for Solving the Problems In order to achieve the above object, the membrane module of the activated sludge treatment device of the present invention is immersed in an aeration tank to arrange a plurality of membrane modules vertically and in parallel, and A membrane module in an activated sludge treatment device in which a constant gap is formed between the membrane modules, and an air diffusing means is provided below the membrane module, the endless frame having a flow passage space for permeate in the center The membrane support is formed by providing a communication hole that communicates the inside and outside of the frame body, and both sides of the membrane support are covered with a filtration membrane, and a filtration membrane is provided between the front and back sides of the membrane support and the filtration membrane. A spacer through which the permeated liquid that has permeated can be provided, and the spacer is formed of a grid net having rigidity.
作用 上記本考案の構成において、外部から連通孔に吸引力を
作用させると、消化処理水は濾過膜を介して吸引され、
固液分離される。すなわち、消化処理水中の汚泥は濾過
膜により捕捉され、他方、濾過膜を透過した洗浄な透過
液は、スペーサを通過して膜支持体の枠体の内側に流入
し、連通孔から外部に吸引される。このとき、脱支持体
の表裏両面を被覆した濾過膜は、吸引力により内方によ
り吸引されるが、スペーサにより支持されるので、両濾
過膜の間にはスペーサにより常に透過液の流路が濾過膜
の全面にわたって維持される。そのため、吸引力は濾過
膜の全面に作用し、濾過膜の有効濾過面積の減少が防止
されるとともに、濾過効率の向上が図られる。また、膜
支持体は構造の簡単な枠体で、厚さが薄く、軽量である
ので、膜モジュールも小形かつ軽量になる。そのため、
濾過膜の洗浄・取替えなどのメンテナンス時に容易に操
作することができる。Action In the above configuration of the present invention, when a suction force is applied from the outside to the communication hole, the digested water is sucked through the filtration membrane,
Solid-liquid separation is performed. That is, the sludge in the digested water is captured by the filtration membrane, while the washed permeate that has passed through the filtration membrane passes through the spacer, flows into the inside of the frame of the membrane support, and is sucked to the outside from the communication hole. To be done. At this time, the filtration membrane covering both the front and back surfaces of the desupport is sucked inward by the suction force, but since it is supported by the spacer, the spacer always provides a permeate flow path between the two filtration membranes. It is maintained over the entire surface of the filtration membrane. Therefore, the suction force acts on the entire surface of the filtration membrane, the reduction of the effective filtration area of the filtration membrane is prevented, and the filtration efficiency is improved. Further, since the membrane support is a frame body having a simple structure, and is thin and lightweight, the membrane module is also small and lightweight. for that reason,
It can be easily operated during maintenance such as cleaning and replacement of the filtration membrane.
実施例 以下、本考案の一実施例を第1図〜第3図に基づいて説
明する。Embodiment An embodiment of the present invention will be described below with reference to FIGS.
本実施例の活性汚泥処理装置においては、第3図に示す
ように、曝気槽21内に上下両面が開放された方形の箱枠
22を設け、箱枠22内に複数個の膜モジュール23を垂直に
一定間隔Aにおいて配列し、膜モジュール23の下方に散
気管24に配置している。曝気槽21には、上方に原水供給
管25が開口し、底部に汚泥引抜きポンプ26を備えた汚泥
引抜き管27が接続されている。また、膜モジュール23に
は、透過液吸引管28を介して透過液集水管29が接続され
ている。透過液集水管29は、途中に吸引ポンプ30を備
え、透過液槽31の上方に開口している。さらに、散気管
24には、給気管32を介してブロワー32が接続されてい
る。In the activated sludge treatment device of this embodiment, as shown in FIG. 3, a rectangular box frame in which both upper and lower sides are opened in the aeration tank 21.
22 is provided, a plurality of membrane modules 23 are vertically arranged in the box frame 22 at a constant interval A, and are arranged in the air diffusing pipe 24 below the membrane module 23. To the aeration tank 21, a raw water supply pipe 25 is opened at the upper side, and a sludge drawing pipe 27 having a sludge drawing pump 26 at the bottom is connected. Further, a permeated liquid collection pipe 29 is connected to the membrane module 23 via a permeated liquid suction pipe 28. The permeated liquid collecting pipe 29 is provided with a suction pump 30 in the middle thereof and opens above the permeated liquid tank 31. In addition, the air diffuser
The blower 32 is connected to the unit 24 via an air supply pipe 32.
膜モジュール23は、第1図および第2図に示すように、
膜支持体34の表裏両面を濾過膜35により被覆し、膜支持
体34の表裏両面と濾過膜35との間にスペーサ36を挿入し
たものである。膜支持体34は、塩化ビニールなどからな
る長方形板の中央部を長方形にくり貫くなどの方法によ
り形成した無端の長方形枠体で、上辺に枠体の内外の連
通する連通孔37を有し、中央部のくり貫き孔は後述する
透過液42の流路空間38を形成する。連通孔37には、透過
液吸引管28を接続する。濾過膜35は、接着剤または両面
接着テープにより膜支持体34に接着する。スペーサ36
は、吸引力を受けた濾過膜35どうしが密着するのを防止
して、透過液42を有効に流路空間38内に流入させるため
に、透過液42の通過可能なものであることが必要で、プ
ラスチック製の格子状ネットなどが適している。The membrane module 23, as shown in FIG. 1 and FIG.
Both sides of the membrane support 34 are covered with a filtration membrane 35, and a spacer 36 is inserted between both sides of the membrane support 34 and the filtration membrane 35. The membrane support 34 is an endless rectangular frame formed by a method such as hollowing out the center of a rectangular plate made of vinyl chloride into a rectangle, and has a communication hole 37 that communicates with the inside and outside of the frame on the upper side. The hollowed-out hole in the central portion forms a flow passage space 38 for the permeated liquid 42 described later. A permeated liquid suction tube 28 is connected to the communication hole 37. The filtration membrane 35 is adhered to the membrane support 34 with an adhesive or a double-sided adhesive tape. Spacer 36
Is required to be able to pass the permeated liquid 42 in order to prevent the permeated liquid 42 from effectively adhering to the flow path space 38 by preventing the filtration membranes 35 that have received suction force from adhering to each other. A plastic grid net is suitable.
次に、上記構成における作用について説明する。Next, the operation of the above configuration will be described.
原水供給管25から原水39を曝気槽21内に供給すると、原
水39は槽内で活性汚泥により消化処理されて消化処理水
40となる。その際、散気管24は、ブロワー33から供給さ
れる空気などの酸素を含有する曝気用気体41を膜モジュ
ール23の間に吹き込み、活性汚泥中の微生物に酸素を供
給する。消化処理水40は、膜モジュール22を介して吸引
ポンプ30により吸引され、膜モジュール23により固液分
離される。すなわち、消化処理水40中の汚泥は濾過膜35
により捕捉され、他方、濾過膜35を濾過した清浄な透過
液42は、スペーサ36を通過して膜支持体34の流路空間38
内に流入し、連通孔37から透過液吸引管28を経由して透
過液集水管29内に吸引され、透過液槽31内に貯留され
る。その際、膜モジュール23の間には曝気用気体41の気
泡のエアリフト作用により消化処理水40の上昇流が生じ
ており、この上昇流が濾過膜35に付着した汚泥を濾過膜
35から離脱させて、濾過膜35の目詰りを防止する。When the raw water 39 is supplied from the raw water supply pipe 25 into the aeration tank 21, the raw water 39 is digested by the activated sludge in the tank to be the digested water.
40. At that time, the air diffuser 24 blows the aeration gas 41 containing oxygen such as air supplied from the blower 33 into the space between the membrane modules 23 to supply oxygen to the microorganisms in the activated sludge. The digested water 40 is sucked by the suction pump 30 through the membrane module 22, and is solid-liquid separated by the membrane module 23. That is, the sludge in the digested water 40 is filtered by the filtration membrane 35.
On the other hand, the clean permeated liquid 42 filtered by the filtration membrane 35 passes through the spacer 36 and the flow passage space 38 of the membrane support 34.
It flows into the inside, is sucked into the permeated liquid collecting pipe 29 from the communication hole 37 via the permeated liquid suction pipe 28, and is stored in the permeated liquid tank 31. At that time, an ascending flow of the digestion-treated water 40 is generated between the membrane modules 23 due to the air-lifting action of the bubbles of the aeration gas 41, and this ascending flow removes the sludge adhering to the filtration membrane 35 to the filtration membrane.
It is separated from 35 to prevent clogging of the filtration membrane 35.
そして、膜モジュール23が消化処理水40の固液分離をす
るとき、濾過膜35は吸引ポンプ30の吸引力により内方に
吸引されるが、スペーサ36により支持されるので、濾過
膜35どうしが密着するのを防止される。そのため、両濾
過膜35の間には、スペーサ36により常に透過液42の流路
が濾過膜35の全面にわたって維持される。したがって、
吸引力は濾過膜35の全面に作用し、濾過膜35の有効濾過
面積の減少が防止されるとともに、濾過効率の向上が図
られる。また、膜支持体34は構造の簡単な枠体で、厚さ
が薄く、軽量であるので、膜モジュール23も小形かつ軽
量になる。そのため、濾過膜35の洗浄・取替えなどのメ
ンテナンス時に容易に操作することができる。Then, when the membrane module 23 performs solid-liquid separation of the digested and treated water 40, the filtration membrane 35 is sucked inward by the suction force of the suction pump 30, but is supported by the spacer 36, so that the filtration membranes 35 are separated from each other. Prevents close contact. Therefore, the flow path of the permeated liquid 42 is always maintained over the entire surface of the filtration membrane 35 by the spacer 36 between the both filtration membranes 35. Therefore,
The suction force acts on the entire surface of the filtration membrane 35 to prevent the effective filtration area of the filtration membrane 35 from decreasing and improve the filtration efficiency. Further, since the membrane support 34 is a frame body having a simple structure, and is thin and lightweight, the membrane module 23 is also small and lightweight. Therefore, the filter membrane 35 can be easily operated during maintenance such as cleaning and replacement.
考案の効果 本考案は、以上説明したように、枠体からなる膜支持体
の表裏両面を被う濾過膜をスペーサにより支持する構成
としたので、吸引力を受けた濾過膜どうしが密着するこ
とが防止される。そのため、吸引力は濾過膜の全面に作
用し、濾過膜の有効濾過面積の減少が防止されるととも
に、濾過効率の向上が図られる。また、膜支持体は構造
の簡単な枠体で、厚さが薄く、軽量であるので、膜モジ
ュールも小形かつ軽量になる。そのため、濾過膜の洗浄
・取替えなどのメンテナンス時に容易に操作することが
できる。Effect of the Invention As described above, according to the present invention, the filtration membrane covering both the front and back sides of the membrane support composed of the frame is supported by the spacers, so that the filtration membranes that have received suction force are closely attached to each other. Is prevented. Therefore, the suction force acts on the entire surface of the filtration membrane, the reduction of the effective filtration area of the filtration membrane is prevented, and the filtration efficiency is improved. Further, since the membrane support is a frame body having a simple structure, and is thin and lightweight, the membrane module is also small and lightweight. Therefore, the filter membrane can be easily operated during maintenance such as cleaning and replacement.
第1図は本考案の一実施例を示す膜モジュールの一部切
欠き正面図、第2図は第1図のII−II線断面図、第3図
は上記膜モジュールを使用した活性汚泥処理装置の全体
構成図、第4図は従来の活性汚泥処理装置の一例を示す
全体構成図である。 23…膜モジュール、34…膜支持体、35…濾過膜、36…ス
ペーサ、37…連通孔、42…透過液。FIG. 1 is a partially cutaway front view of a membrane module showing an embodiment of the present invention, FIG. 2 is a sectional view taken along the line II-II of FIG. 1, and FIG. 3 is an activated sludge treatment using the membrane module. FIG. 4 is an overall configuration diagram of the device, and FIG. 4 is an overall configuration diagram showing an example of a conventional activated sludge treatment device. 23 ... Membrane module, 34 ... Membrane support, 35 ... Filtration membrane, 36 ... Spacer, 37 ... Communication hole, 42 ... Permeate.
Claims (1)
垂直に、かつ平行に配置するとともに、隣接する膜モジ
ュールの相互間に一定の間隙を形成し、膜モジュールの
下方に散気手段を設ける活性汚泥処理装置における膜モ
ジュールであって、中央部に透過液の流路空間を有する
無端の枠体に、枠体の内外を連通する連通孔を設けて膜
支持体を形成し、膜支持体の表裏両面を濾過膜により被
覆し、膜支持体の表裏両面と濾過膜との間に濾過膜を透
過した透過液の通過可能なスペーサを設け、このスペー
サを剛性を有する格子状ネットで形成したことを特徴と
する活性汚泥処理装置の膜モジュール。1. A plurality of membrane modules are vertically and parallelly arranged by immersing the membrane modules in an aeration tank, and a constant gap is formed between adjacent membrane modules, and an air diffusing means is provided below the membrane module. A membrane module in an activated sludge treatment device, wherein an endless frame body having a flow passage space for permeate in a central portion is provided with a communication hole for communicating the inside and outside of the frame body to form a membrane support, Both the front and back surfaces of the support are covered with a filtration membrane, and a spacer is provided between the front and back surfaces of the membrane support and the filtration membrane to allow passage of the permeate that has permeated the filtration membrane. A membrane module for an activated sludge treatment device characterized by being formed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1989069938U JPH0713832Y2 (en) | 1989-06-15 | 1989-06-15 | Membrane module of activated sludge treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1989069938U JPH0713832Y2 (en) | 1989-06-15 | 1989-06-15 | Membrane module of activated sludge treatment equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0311426U JPH0311426U (en) | 1991-02-05 |
| JPH0713832Y2 true JPH0713832Y2 (en) | 1995-04-05 |
Family
ID=31605676
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1989069938U Expired - Lifetime JPH0713832Y2 (en) | 1989-06-15 | 1989-06-15 | Membrane module of activated sludge treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0713832Y2 (en) |
-
1989
- 1989-06-15 JP JP1989069938U patent/JPH0713832Y2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0311426U (en) | 1991-02-05 |
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