JPH0722750B2 - Membrane module of activated sludge treatment equipment - Google Patents

Membrane module of activated sludge treatment equipment

Info

Publication number
JPH0722750B2
JPH0722750B2 JP1137256A JP13725689A JPH0722750B2 JP H0722750 B2 JPH0722750 B2 JP H0722750B2 JP 1137256 A JP1137256 A JP 1137256A JP 13725689 A JP13725689 A JP 13725689A JP H0722750 B2 JPH0722750 B2 JP H0722750B2
Authority
JP
Japan
Prior art keywords
membrane
filtration
permeate
membrane module
activated sludge
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
JP1137256A
Other languages
Japanese (ja)
Other versions
JPH034982A (en
Inventor
正史 師
清司 和泉
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
Application filed by Kubota Corp filed Critical Kubota Corp
Priority to JP1137256A priority Critical patent/JPH0722750B2/en
Publication of JPH034982A publication Critical patent/JPH034982A/en
Publication of JPH0722750B2 publication Critical patent/JPH0722750B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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)
  • Activated Sludge Processes (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、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を配置している。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. An air diffuser 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を透過した清浄な透過膜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り消化処理
水16の上昇流が生じており、この上昇流によって濾過膜
8に対する汚泥の付着を困難にして、濾過膜8の目詰り
を防止していた。
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 filter membrane 8, while the clean permeable membrane 18 that has permeated the filter 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 is generated between the membrane modules 3 due to the air lift action of the bubbles of the aeration gas 17, and this ascending flow makes it difficult to attach the sludge to the filtration film 8 No. 8 clogging was prevented.

発明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、構造が
複雑で、厚さが厚いため、膜モジュール3が大形かつ高
価になり、取扱いも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 permeated liquid 18 between them. 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. Furthermore, since the structure is complicated and the thickness is large, the membrane module 3 becomes large and expensive, and it is not easy to handle.

本発明は、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。
It is an object of the present invention 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、本発明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、剛性を有する板状の膜支持ネ
ットの表裏両面を覆って濾過膜を設け、表裏の濾過膜の
間に膜支持ネットにより透過液の流路間隙を形成し、膜
支持ネットの上端縁を透過液吸引管に管軸心方向に沿っ
て設けたスリット内に挿着し、袋状をなす濾過膜の上端
開口を吸引管に接着して固定し、膜支持ネットの下端部
を濾過膜と重ね合わせて支持棒に巻回して固定し、前記
流路間隙を透過液吸引管に連通させ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 vertically and parallelly arrange a plurality of membrane modules, and adjacent to each other. A membrane module in an activated sludge treatment device in which a uniform gap is formed between the membrane modules to be provided, and an air diffusing means is provided below the membrane module, and the both sides of a rigid plate-shaped membrane support net are covered. A filtration membrane is provided, and a permeate flow path gap is formed by a membrane support net between the front and back filtration membranes, and the upper edge of the membrane support net is placed in a slit provided in the permeate suction pipe along the tube axial direction. The upper end opening of the bag-shaped filter membrane is fixed by adhering it to the suction tube, and the lower end of the membrane support net is superposed on the filter membrane and wound around the support rod to be fixed. It is configured to communicate with the permeate suction tube It is a thing.

作用 上記本発明の構成において、透過液吸引管に吸引力を作
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、濾過膜を透過した清浄な透過液
は、濾過膜の間に膜支持ネットにより形成された流路間
隙を経由して、流路間隙と連通する透過液吸引管内に吸
引される。このとき、膜支持ネット両面の濾過膜は、吸
引力により内方に吸引されるが、膜支持ネットに保持さ
れるので、両濾過膜の間には膜支持ネットにより常に流
路間隙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、濾過膜は膜支持ネットにより直接保持さ
れるので、構造が簡単になる上に、膜モジュールの厚さ
が薄くなる。したがって、膜モジュールは、小形かつ安
価になり、取扱いも容易になる。
Action In the above configuration of the present invention, when a suction force is applied to the permeated liquid suction tube, the digested water is sucked through the filtration membrane and solid-liquid separated. That is, the sludge in the digested water is captured by the filtration membrane, while the clean permeate that has permeated the filtration membrane passes through the flow passage gap formed by the membrane support net between the filtration membranes, The liquid is sucked into the permeated liquid suction pipe communicating with. At this time, the filtration membranes on both sides of the membrane support net are sucked inward by the suction force, but since they are held by the membrane support net, a flow path gap is always provided between the filtration membranes by the membrane support net. Maintained over the entire surface of. 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 filtration membrane is directly held by the membrane supporting net, the structure is simple and the thickness of the membrane module is thin. Therefore, the membrane module is small and inexpensive, and is easy to handle.

実施例 以下、本発明の一実施例を第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. 1 to 3.

本実施例の活性汚泥処理装置においては、第1図に示す
ように、曝気槽21内に箱枠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をおいて配列し、
膜モジュール23の下方に散気管24を配置している。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。箱枠22は、方形で、上下両面が開放されている。膜
モジュール23は、第2図および第3図に示すように、方
形板状のプラスチック製膜支持ネット28の両面を濾過膜
29により被覆し、膜支持ネット28の上端縁を透過液吸引
管30に管軸方向に設けたスリット31内に挿着し、膜支持
ネット28の下端部を濾過膜29と重ね合わせて支持棒32に
巻き付け、固着したものである。膜支持ネット28は濾過
膜29の間に透過液の流路間隙を形成し、この流路間隙は
スリット31内に挿着した膜支持ネット28の上端縁を介し
て透過液吸引管30に連通する。濾過膜29は、袋状に形成
し、上端の開口周縁部を透過液吸引管30に接着剤で接着
する。透過液吸引管30は、両端部が膜支持ネット28の両
側縁から外方に突出し、一端が開口し、他端は閉じてい
る。支持棒32の両端部も、膜支持ネット28の両側縁から
外方に突出している。膜モジュール23は、透過液吸引管
30および支持棒32の突出した両端部を介して箱枠22に固
定し、透過液吸引管30の開口側端部を透過液集水管33に
接続する。透過液集水管33は、途中に吸引ポンプ34を備
え、透過液槽35の上方に開口している。散気管24は、給
気管36を介してブロワー37に接続する。
In the activated sludge treatment device of this embodiment, as shown in FIG. 1, a box frame 22 is provided in the aeration tank 21, and a plurality of membrane modules 23 are vertically arranged at a constant interval A in the box frame 22. Array
An air diffuser 24 is arranged 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. The box frame 22 has a rectangular shape and both upper and lower sides are open. The membrane module 23, as shown in FIG. 2 and FIG. 3, has both sides of a rectangular plate-shaped plastic membrane supporting net 28 for filtering membranes.
29, the upper edge of the membrane support net 28 is inserted into a slit 31 provided in the permeate suction tube 30 in the tube axial direction, and the lower end of the membrane support net 28 is superposed on the filtration membrane 29 to form a support rod. It is wrapped around 32 and fixed. The membrane support net 28 forms a permeate flow passage gap between the filtration membranes 29, and this flow passage gap communicates with the permeate suction pipe 30 via the upper end edge of the membrane support net 28 inserted in the slit 31. To do. The filtration membrane 29 is formed in a bag shape, and the periphery of the opening at the upper end is adhered to the permeated liquid suction tube 30 with an adhesive. Both ends of the permeated liquid suction tube 30 project outward from both side edges of the membrane support net 28, one end is open, and the other end is closed. Both ends of the support rod 32 also project outward from both side edges of the membrane support net 28. The membrane module 23 is a permeate suction tube.
The support 30 is fixed to the box frame 22 via the projecting ends of the support rod 32, and the end of the permeate suction pipe 30 on the opening side is connected to the permeate collecting pipe 33. The permeated liquid collecting pipe 33 is provided with a suction pump 34 in the middle thereof and opens above the permeated liquid tank 35. The air diffuser 24 is connected to the blower 37 via the air supply pipe 36.

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38を曝気槽21内に供給すると、原
水38は槽内で活性汚泥により消化処理されて消化処理水
39となる。その際、散気管24は、ブロワー37から供給さ
れる空気などの酸素を含有する曝気用気体40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39は、膜モジュール23を介して吸引
ポンプ34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39中の汚泥は濾過膜29
により捕捉され、他方、濾過膜29を透過した清浄な透過
液41は、濾過膜29の間に膜支持ネット28により形成され
た流路間隙を経由して、流路間隙と連通する透過液吸引
管30内に吸引され、透過液集水管33を経由して透過液槽
35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40の気泡のエアリフト作用により消化処理水39
の上昇流が生じており、この上昇流が濾過膜29に付着し
た汚泥を濾過膜29から離脱させて、濾過膜29の目詰りを
防止する。
When the raw water 38 is supplied into the aeration tank 21 from the raw water supply pipe 25, the raw water 38 is digested by the activated sludge in the tank and the digested water is obtained.
39. At that time, the air diffuser 24 blows an aeration gas 40 containing oxygen such as air supplied from the blower 37 between the membrane modules 23 to supply oxygen to the microorganisms in the activated sludge. The digested water 39 is sucked by the suction pump 34 through the membrane module 23, and is solid-liquid separated by the membrane module 23. That is, the sludge in the digested water 39 is filtered by the filtration membrane 29.
On the other hand, the clean permeated liquid 41 that has been captured by the filter membrane 29 and has permeated through the filtration membrane 29 passes through the flow passage gap formed by the membrane support net 28 between the filtration membranes 29, and the permeated liquid suction that communicates with the flow passage gap The permeate tank is sucked into the pipe 30 and passes through the permeate collection pipe 33.
Stored in 35. At that time, the digested water 39 is provided between the membrane modules 23 by the air lift action of the bubbles of the aeration gas 40.
Is generated, the sludge attached to the filtration membrane 29 is separated from the filtration membrane 29, and the clogging of the filtration membrane 29 is prevented.

そして、膜モジュール23が消化処理水39の固液分離をす
るとき、膜支持ネット28の両面の濾過膜29は、吸引力に
より内方に吸引されるが、膜支持ネット28に保持される
ので、両濾過膜29の間には膜支持ネット28により常に流
路間隙が濾過膜29の全面にわたって維持される。そのた
め、吸引力は濾過膜29の全面に作用し、濾過膜29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、濾過膜29は膜支持ネット28により直
接保持されるので、構造が簡単になる上に、膜モジュー
ル23の厚さが薄くなる。したがって、膜モジュール23
は、小形かつ安価になり、取扱いも容易になる。
When the membrane module 23 performs solid-liquid separation of the digested water 39, the filtration membranes 29 on both sides of the membrane supporting net 28 are sucked inward by the suction force, but are retained by the membrane supporting net 28. Between the two filtration membranes 29, the membrane support net 28 always maintains a flow path gap over the entire surface of the filtration membrane 29. Therefore, the suction force acts on the entire surface of the filtration membrane 29, the reduction of the effective filtration area of the filtration membrane 29 is prevented, and the filtration efficiency is improved. Further, since the filtration membrane 29 is directly held by the membrane support net 28, the structure is simplified and the thickness of the membrane module 23 is reduced. Therefore, the membrane module 23
Is smaller, cheaper, and easier to handle.

発明の効果 本発明は、以上説明したように、膜支持ネットの両面を
濾過膜により被覆して、濾過膜の間に膜支持ネットによ
り透過液の流路間隙を形成したので、濾過膜全面にわた
って流路間隙が形成され、吸引力が濾過膜全面に作用す
る。したがって、濾過膜の有効濾過面積の減少が防止さ
れるとともに、濾過効率の向上を図ることができる。ま
た、濾過膜は膜支持ネットにより直接保持されるので、
構造が簡単になる上に、膜モジュールの厚さが薄くな
る。したがって、膜モジュールは、小形かつ安価にな
り、取扱いも容易になる。
As described above, according to the present invention, both sides of the membrane supporting net are covered with the filtration membrane, and the permeate passage gap is formed between the filtration membranes by the membrane supporting net. A flow path gap is formed, and the suction force acts on the entire surface of the filtration membrane. Therefore, it is possible to prevent the effective filtration area of the filtration membrane from decreasing and improve the filtration efficiency. Also, since the filtration membrane is directly held by the membrane support net,
In addition to the simple structure, the thickness of the membrane module is reduced. Therefore, the membrane module is small and inexpensive, and is easy to handle.

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

第1図は本発明の一実施例を示す活性汚泥処理装置の全
体構成図、第2図は第1図における膜モジュールの正面
図、第3図は第2図のIII-III線断面図、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、28……膜支持ネット、29……濾過
膜、30……透過液吸引管、31……スリット、41……透過
液。
FIG. 1 is an overall configuration diagram of an activated sludge treatment device showing an embodiment of the present invention, FIG. 2 is a front view of the membrane module in FIG. 1, FIG. 3 is a sectional view taken along line III-III of FIG. FIG. 4 is an overall configuration diagram showing an example of a conventional activated sludge treatment device. 23 …… Membrane module, 28 …… Membrane support net, 29 …… Filtration membrane, 30 …… Permeate suction tube, 31 …… Slit, 41 …… Permeate.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】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、剛性を有する板状の膜支持ネットの
表裏両面を覆って濾過膜を設け、表裏の濾過膜の間に膜
支持ネットにより透過液の流路間隙を形成し、膜支持ネ
ットの上端縁を透過液吸引管に管軸心方向に沿って設け
たスリット内に挿着し、袋状をなす濾過膜の上端開口を
吸引管に接着して固定し、膜支持ネットの下端部を濾過
膜と重ね合わせて支持棒に巻回して固定し、前記流路間
隙を透過液吸引管に連通させ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, in which a filtration membrane is provided by covering both front and back sides of a rigid plate-shaped membrane support net, and a permeate flow path gap is provided between the front and back filtration membranes by the membrane support net. The upper end edge of the membrane support net is inserted into the slit provided in the permeate suction tube along the axial direction of the permeate, and the upper end opening of the bag-shaped filter membrane is fixed by adhering to the suction tube. A membrane module for an activated sludge treatment device, characterized in that the lower end of the membrane supporting net is superposed on a filtration membrane, wound around a supporting rod and fixed, and the channel gap is communicated with a permeate suction pipe.
JP1137256A 1989-05-29 1989-05-29 Membrane module of activated sludge treatment equipment Expired - Lifetime JPH0722750B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1137256A JPH0722750B2 (en) 1989-05-29 1989-05-29 Membrane module of activated sludge treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1137256A JPH0722750B2 (en) 1989-05-29 1989-05-29 Membrane module of activated sludge treatment equipment

Publications (2)

Publication Number Publication Date
JPH034982A JPH034982A (en) 1991-01-10
JPH0722750B2 true JPH0722750B2 (en) 1995-03-15

Family

ID=15194413

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1137256A Expired - Lifetime JPH0722750B2 (en) 1989-05-29 1989-05-29 Membrane module of activated sludge treatment equipment

Country Status (1)

Country Link
JP (1) JPH0722750B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2646299B2 (en) * 1991-03-19 1997-08-27 株式会社荏原製作所 Filtration and separation equipment
JP4859802B2 (en) 2007-09-28 2012-01-25 株式会社内田洋行 Hanging device
WO2010016091A1 (en) * 2008-08-05 2010-02-11 株式会社早川バルブ製作所 Switching valve device

Also Published As

Publication number Publication date
JPH034982A (en) 1991-01-10

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