JPH034982A - Membrane module for activated sludge treating apparatus - Google Patents

Membrane module for activated sludge treating apparatus

Info

Publication number
JPH034982A
JPH034982A JP1137256A JP13725689A JPH034982A JP H034982 A JPH034982 A JP H034982A JP 1137256 A JP1137256 A JP 1137256A JP 13725689 A JP13725689 A JP 13725689A JP H034982 A JPH034982 A JP H034982A
Authority
JP
Japan
Prior art keywords
membrane
filter
net
filtration
permeate
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.)
Granted
Application number
JP1137256A
Other languages
Japanese (ja)
Other versions
JPH0722750B2 (en
Inventor
Masashi Moro
正史 師
Seiji Izumi
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

Abstract

PURPOSE:To contrive the improvement of filtering efficiency by a method wherein filter membranes are provided covering each side of a membrane supporting net, filtrate passageways are defined between the filter membranes by the membrane supporting net and the membrane supporting net is engaged at one end into a slit provided in a filtrate suction pipe. CONSTITUTION:The sludge in a digesting water 39 is captured by filter membranes 29, while a clean filtrate 41 separated by the filter membranes 29 is sucked through passageways defined on a membrane supporting net 28 between the filter membrane 29 into a filtrate suction pipe 30 in communication with the passageways and stored in a filtrate tank 35 through a filtrate collecting pipe 33. When membrane modules 23 effect solid-liquid separation of the digesting water 39, the filter membrane 29 on each side of the net 28 are sucked inwardly by the sucking force but held by the net 28 and, therefore, the passageways are always maintained by the net 28 between both the filter membranes 29 over the entire surfaces of the filter membranes. For this reason, the sucking force is exerted over the entire surface of the filter membrane 29, thereby preventing the decrease of the effective filter area of the filter membrane 29 with an improved filtering efficiency.

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。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a membrane module for an activated sludge treatment apparatus 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に接続さ九ている。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−14に接続されている。
Conventional technology Conventionally, in activated sludge treatment equipment for organic wastewater,
For example, as shown in FIG. 4, a rectangular box frame 2 with open top and bottom surfaces is provided in an aeration tank 1, and a plurality of membrane modules 3 are arranged vertically within the box frame 2 at regular intervals a. , a diffuser pipe 4 is arranged below the membrane module 3. 5 is a raw water supply pipe opening into 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 constructed by covering both sides of a membrane support 7 curved in an uneven shape with a filtration membrane 8, and a permeate collection pipe is connected to the permeate suction pipe 9 connected to the upper end of the membrane support 7. There are 9 connected to 10. The permeated liquid collection pipe 10 is provided with a suction pump 11 in the middle and opens into a permeated liquid tank 12 . The air diffuser 4 is connected to a blower 14 via an air supply pipe 13.

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−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6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。
The raw water 15 supplied into the aeration tank 1 from the raw water supply pipe 5 is
The water is digested with activated sludge in the tank and becomes digested water 16. At that time, the aeration pipe 4 blows an aeration gas 17 containing oxygen, such as air supplied from the blower 14, between the membrane modules 3 to supply oxygen to the microorganisms in the activated sludge. is sucked by the suction pump 11 through the membrane module 3, and is separated into solid and liquid by the membrane module 3.

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液18は
、透過液吸引管9から透過液集水管IO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。
That is, the sludge in the digested water 16 is captured by the filtration membrane 8, while the clean permeate 18 that has passed through the filtration membrane 8 is passed from the permeate suction pipe 9 to the permeate collection pipe IO to the permeate tank. It is stored in 12. At this time, an upward flow of the digested water 16 is generated between the membrane modules 3 due to the air lift effect of the bubbles of the aeration gas 17, and this upward flow makes it difficult for sludge to adhere to the filtration membrane 8. 8 was prevented from clogging.

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。Problems that the invention aims to solve However, in the conventional membrane module 3 described above.

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。
In the suction state, a part of the filtration membrane 8 comes into close contact with the convex part of the membrane support 7, and there is no flow path for the permeated liquid 18 between the two, and the suction force no longer acts effectively on that part, which prevents filtration. Function deteriorates. Therefore, there was a problem that the effective filtration area of the filtration membrane 8 was reduced and the filtration efficiency was lowered. Furthermore, since the structure is complicated and the membrane module 3 is thick, there are problems in that the membrane module 3 is large and expensive, and 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。
The present invention aims to solve these problems by improving conventional membrane modules.

課題を解決するための手段 上記目的を達成するために1本発明の活性汚泥処理装置
の膜モジュールは、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。
Means for Solving the Problems In order to achieve the above objects, the membrane module of the activated sludge treatment apparatus of the present invention is provided with filtration membranes covering both the front and back sides of a membrane support net, and a membrane support between the front and back filtration membranes. The net forms a flow path gap for the permeate.

膜支持ネットの一端縁を透過液吸引管に設けたスリット
内に挿着して、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。
One end edge of the membrane support net is inserted into a slit provided in the permeate suction tube, so that the flow path gap is communicated with the permeate suction tube.

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、流路間隙と連通ずる透過液吸引管内に吸
引される。
Function In the above structure of the present invention, when a suction force is applied to the permeate suction tube, the digested water is suctioned through the filtration membrane and separated into solid and liquid. That is, the sludge in the digestion water is captured by the filtration membrane, while the clean permeate that has passed through the filtration membrane passes through the channel gap formed by the membrane support net between the filtration membranes. The permeate is sucked into the permeate suction tube that communicates with the permeate.

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、
面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。
At this time, the filtration membranes on both sides of the membrane support net are sucked inward by the suction force, but because they are held by the membrane support net,
Between the surface filtration membranes, a flow path gap is always maintained over the entire surface of the filtration membranes by a membrane support net. Therefore, the suction force acts on the entire surface of the filtration membrane, preventing a decrease in the effective filtration area of the filtration membrane, and improving filtration efficiency. Furthermore, since the filtration membrane is directly supported by the membrane support net, the structure is simple and the thickness of the membrane module is reduced.

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。
Therefore, the membrane module becomes smaller, cheaper, and easier 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。
EXAMPLE Hereinafter, an example of the present invention will be described based on 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に連通ずる。濾過膜29は1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6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。
In the activated sludge treatment apparatus of this embodiment, as shown in FIG. A diffuser pipe 24 is arranged below the membrane module 23. A raw water supply pipe 25 opens upward to the aeration tank 21, and a sludge drawing pipe 27 equipped with a sludge drawing pump 26 is connected to the bottom. The box frame 22 is rectangular and both upper and lower sides are open. As shown in FIGS. 2 and 3, the membrane module 23 has a rectangular plate-shaped plastic membrane support net 28 covered with filtration membranes 29 on both sides, and the upper edge of the membrane support net 28 connected to a permeate suction tube. 30 into a slit 31 provided in the tube axis direction, the lower end of the membrane support net 28 is overlapped with the filtration membrane 29 and wrapped around the support rod 32,
It is fixed. The membrane support net 28 forms a flow path gap for the permeate between the filtration membranes 29, and this flow path gap is connected to the permeate suction tube 30 via the upper edge of the membrane support net 28 inserted into the slit 31. It goes through. The filtration membrane 29 is formed in the shape of a bag, and the upper opening periphery is bonded to the permeate suction tube 30 with an adhesive. Both ends of the permeate suction tube 30 protrude outward from both side edges of the membrane support net 28, one end being open and the other end being closed. Both ends of the support rod 32 are also connected to the membrane support net 28.
It protrudes outward from both side edges. The membrane module 23 is fixed to the box frame 22 via the protruding ends of the permeate suction tube 30 and the support rod 32, and the six permeate tubes are connected to the open end of the permeate suction tube 30 to the permeate collection tube 33. Liquid collection pipe 33
is equipped with a suction pump 34 in the middle and opens above the permeate tank 35.

散気管24は、給気管36を介してブロワ−37に接続
する。
The air diffuser pipe 24 is connected to a blower 37 via an 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 explained.

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−
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の間に膜支持ネント28により形成された流路間隙
を経由して、流路間隙と連通ずる透過液吸引管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3
9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 raw water 38 is supplied into the aeration tank 21 from the raw water supply pipe 25, the raw water 38 is digested with activated sludge in the tank and becomes digested water 39. At that time, the diffuser pipe 24
Aeration gas 40 containing oxygen such as air supplied from 37 is blown between the membrane modules 23 to supply oxygen to microorganisms in the activated sludge. The digested water 39 is sucked through the membrane module 23 by the suction pump 34, and is separated into solid and liquid by the membrane module 23. That is, the sludge in the digested water 39 is captured by the filtration membrane 29, and on the other hand, the clean permeate 41 that has passed through the filtration membrane 29 flows through the channel gap formed by the membrane support member 28 between the filtration membranes 29. The permeate is sucked into the permeate suction pipe 30 communicating with the flow path gap, and stored in the permeate tank 35 via the permeate collection pipe 33 . At that time, between the membrane modules 23, the digested water 3
9 is generated, and this upward flow causes the sludge adhering to the filtration membrane 29 to separate from the filtration membrane 29, thereby preventing the filtration membrane 29 from clogging.

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、両雄過膜29の間には膜支持ネット2
8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8そのため、吸引力は濾過膜29の全面に作用
し、ilJ!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[
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 support net 28
Although it is sucked inward by the suction force, it is held by the membrane support net 28, so the membrane support net 2 is placed between the two male membranes 29.
8, the flow path gap is always maintained over the entire surface of the filtration membrane 29. Therefore, the suction force acts on the entire surface of the filtration membrane 29, and ilJ! A decrease in the effective filtration area of the filtration membrane 29 is prevented, and the filtration efficiency is improved. In addition, filtration [
29 is directly held by the membrane support net 28, which not only simplifies the structure but also reduces the thickness of the membrane module 23. Therefore, the membrane module 23 is small, inexpensive, and easy 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。
Effects of the Invention As explained above, in the present invention, both sides of the membrane support net are covered with the filtration membrane, and a flow path gap for the permeated liquid is formed between the filtration membranes by the membrane support net. A channel gap is formed, and suction force acts on the entire surface of the filtration membrane. Therefore, the effective filtration area of the filtration membrane is prevented from decreasing, and the filtration efficiency can be improved. In addition, since the filtration membrane is directly held by the membrane support net,
In addition to simplifying the structure, the thickness of the membrane module can also be reduced. Therefore, the membrane module becomes smaller and cheaper;
It also becomes easier to handle.

【図面の簡単な説明】[Brief explanation of the drawing]

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■−■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、2
9・・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 apparatus showing an embodiment of the present invention, FIG. 2 is a front view of the membrane module in FIG. 1, and FIG. 3 is a sectional view taken along the line ■-■ in FIG. FIG. 4 is an overall configuration diagram showing an example of a conventional activated sludge treatment apparatus. 23... Membrane module, 28... Membrane support net, 2
9...filtration membrane, 30...permeate suction tube, 31...
Slit, 41... Permeated liquid.

Claims (1)

【特許請求の範囲】[Claims] 1、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、膜支持ネットの一端縁を透過液吸引管に設け
たスリット内に挿着して、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 filtration membrane is provided covering both the front and back sides of the membrane support net, a flow path gap for the permeate is formed by the membrane support net between the front and back filtration membranes, and one end edge of the membrane support net is provided on the permeate suction tube. 1. A membrane module for an activated sludge treatment apparatus, characterized in that the membrane module is inserted into a slit in which the flow path is in communication 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 true JPH034982A (en) 1991-01-10
JPH0722750B2 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)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04290529A (en) * 1991-03-19 1992-10-15 Ebara Infilco Co Ltd Filtration separator
JP4757315B2 (en) * 2008-08-05 2011-08-24 株式会社早川バルブ製作所 Switching valve device
US8453989B2 (en) 2007-09-28 2013-06-04 Uhchida Yoko Co., Ltd. Suspension device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04290529A (en) * 1991-03-19 1992-10-15 Ebara Infilco Co Ltd Filtration separator
US8453989B2 (en) 2007-09-28 2013-06-04 Uhchida Yoko Co., Ltd. Suspension device
JP4757315B2 (en) * 2008-08-05 2011-08-24 株式会社早川バルブ製作所 Switching valve device

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JPH0722750B2 (en) 1995-03-15

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