JPH0356192A - Washing of membrane module with chemical - Google Patents
Washing of membrane module with chemicalInfo
- Publication number
- JPH0356192A JPH0356192A JP1189798A JP18979889A JPH0356192A JP H0356192 A JPH0356192 A JP H0356192A JP 1189798 A JP1189798 A JP 1189798A JP 18979889 A JP18979889 A JP 18979889A JP H0356192 A JPH0356192 A JP H0356192A
- Authority
- JP
- Japan
- Prior art keywords
- valve
- treatment tank
- membrane module
- tank
- filtration
- 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
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 53
- 239000000126 substance Substances 0.000 title claims abstract description 44
- 238000005406 washing Methods 0.000 title claims abstract description 17
- 238000001914 filtration Methods 0.000 claims abstract description 50
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000007788 liquid Substances 0.000 claims abstract description 32
- 230000000813 microbial effect Effects 0.000 claims abstract description 27
- 239000011259 mixed solution Substances 0.000 claims abstract description 26
- 239000000243 solution Substances 0.000 claims abstract description 22
- 244000005700 microbiome Species 0.000 claims abstract description 11
- 238000004140 cleaning Methods 0.000 claims description 25
- 238000004891 communication Methods 0.000 claims description 23
- 239000010865 sewage Substances 0.000 claims description 21
- 238000005192 partition Methods 0.000 claims description 11
- 238000005273 aeration Methods 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 5
- 239000003795 chemical substances by application Substances 0.000 claims description 4
- 230000003472 neutralizing effect Effects 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims description 3
- 238000007664 blowing Methods 0.000 claims description 2
- 239000010802 sludge Substances 0.000 abstract description 27
- 239000000706 filtrate Substances 0.000 abstract 3
- 239000012466 permeate Substances 0.000 description 5
- 239000012141 concentrate Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 241000218691 Cupressaceae Species 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
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)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は,原水を微生物処理した後の混合溶液をろ過膜
によりろ過処理する汚水処理装置における膜モジュール
の薬品洗浄方法に関する。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method for chemically cleaning a membrane module in a sewage treatment apparatus in which a mixed solution after microbial treatment of raw water is filtered through a filtration membrane.
従来の技術
従来より、上記のような汚水処理装置においては、たと
えば第2図に示すように、微生物処理槽1内にろ過膜を
有する膜モジュール2が複数個設けられるとともに、膜
モジュール2の下方に曝気用散気管3が設けられていた
。そして、汚水の原水4は、微生物処理槽1内に供給さ
れて微生物処理され、微生物との混合溶液5となる。こ
の混合溶液5は、散気管3から吹き出される曝気用空気
6の気泡により上昇流となり、膜モジュール2によりろ
過処理されて濃縮液と透過液とに分離され、濃縮液はさ
らに上昇して第2図中の矢印方向に循環し、膜モジュー
ル2内の透過液は吸引ポンプ(図示省略)により外部に
排出されるのである。Conventionally, in the above-mentioned sewage treatment equipment, for example, as shown in FIG. A diffuser pipe 3 for aeration was installed. The raw sewage water 4 is then supplied into the microbial treatment tank 1 and treated with microorganisms to form a mixed solution 5 with microorganisms. This mixed solution 5 becomes an upward flow due to the bubbles of the aeration air 6 blown out from the aeration pipe 3, is filtered by the membrane module 2, and is separated into a concentrated liquid and a permeated liquid, and the concentrated liquid further rises to form a permeated liquid. The permeate in the membrane module 2 circulates in the direction of the arrow in Figure 2, and is discharged to the outside by a suction pump (not shown).
発明が解決しようとする課題
ところで、膜モジュール2は、使用するにつれて混合溶
液5中の固形分により次第に目詰りするので、薬液によ
り定期的に洗浄する必要がある。Problems to be Solved by the Invention By the way, as the membrane module 2 is used, it gradually becomes clogged with the solid content in the mixed solution 5, so it is necessary to periodically clean it with a chemical solution.
しかし、上記従来の構成においては、膜モジュール2を
洗浄する場合、活性汚泥中の微生物が薬液により死滅し
ないよう膜モジュール2または微生物を槽外に取り出し
て行なう必要があるため、洗浄に手間取るだけでなく,
汚水処理装置の運転休止時間が長引くという問題があっ
た。However, in the conventional configuration described above, when cleaning the membrane module 2, it is necessary to remove the membrane module 2 or the microorganisms from the tank so that the microorganisms in the activated sludge are not killed by the chemical solution, so cleaning only takes time. Without,
There was a problem in that the sewage treatment equipment was out of operation for a long time.
本発明は、このような従来の問題点を解消して、膜モジ
ュールおよび微生物のいずれをも外部に取り出すことな
く薬品洗浄できる方法を提供することを目的とする。It is an object of the present invention to provide a method that eliminates these conventional problems and allows chemical cleaning to be performed without taking out either the membrane module or the microorganisms to the outside.
課題を解決するための手段
上記目的を達成するために、本発明の膜モジュールの薬
品洗浄方法は,原水を微生物処珊する微生物処理槽と、
微生物処理後の混合溶液をろ過膜を有する膜モジュール
によりろ過処理するろ過処理槽とを仕切壁を介して仕切
壁越しに連通可能に併設し、微生物処理槽の底部に第1
バルブを接続し、ろ過処理槽の内部に複数個の膜モジュ
ールおよび膜モジュールの下方の曝気用散気管を設け、
前記ろ過処理槽の底部に第2バルブおよび第3バルブを
直列に接続し、第1バルブに、第2バルブとの間に第4
バルブを有する第1連通管と、第3バルブとの間にポン
プを有する第2連通管とを接続し、第2連通管のポンプ
と第3パルプとの中間に、第5パルプを有する移送管と
排水バルブを有する排水管とを接続し、移送管の他端を
微生物処理槽上に開口して汚水処理装置を構成するとと
もに、
微生物処理槽への原水の供給を停止し、かつ第1バルブ
、第2バルブおよび第3バルブ以外のバルブを閉じる第
1工程と、ポンプにより微生物処理槽内の混合溶液の一
部をろ過処理槽内に送りながら、混合溶液を膜モジュー
ルによりろ過処理して濃縮液と透過液とに分離し、膜モ
ジュール内の透過液を外部に排出することにより微生物
処理槽内の混合溶液を減量させる第2工程と、第1バル
ブおよび第3バルブを閉じるとともに、第2バルブ、第
4バルブおよび第5バルブを開き、ポンプによりろ過処
理槽内の濃縮液をすべて微生物処理槽内に移送する第3
工程と、すべてのバルブを閉じ、ろ過処理槽内に洗浄水
を入れて散気管から空気を吹き込むことにより膜モジュ
ールを水洗した後、第2バルブ、第3バルブおよび排水
バルブを開いて洗浄水を排出する第4工程と、すべての
バルブを閉じ、ろ過処理槽内に薬液を入れて膜モジュー
ルを薬品洗浄した後、薬液中に中和剤を入れて薬液を中
和させる第5工程と、第1バルブ、第2バルブおよび第
4バルブを開いて汚水処理装置の運転を再開する第6工
程とを有するようにしたものである。Means for Solving the Problems In order to achieve the above object, the chemical cleaning method for membrane modules of the present invention includes a microbial treatment tank for microbial treatment of raw water;
A filtration treatment tank in which a mixed solution after microbial treatment is filtered by a membrane module having a filtration membrane is installed so as to be able to communicate with it through a partition wall, and a first filter is installed at the bottom of the microbial treatment tank.
A valve is connected, and a plurality of membrane modules and an aeration diffuser pipe below the membrane module are installed inside the filtration treatment tank.
A second valve and a third valve are connected in series to the bottom of the filtration treatment tank, and a fourth valve is connected between the first valve and the second valve.
A first communication pipe having a valve and a second communication pipe having a pump are connected between the third valve and a transfer pipe having a fifth pulp between the pump of the second communication pipe and the third pulp. and a drain pipe having a drainage valve, and the other end of the transfer pipe is opened above the microbial treatment tank to constitute a sewage treatment device, and the supply of raw water to the microbial treatment tank is stopped, and the first valve is opened. , a first step of closing valves other than the second valve and the third valve, and a part of the mixed solution in the microbial treatment tank is sent into the filtration treatment tank by a pump, and the mixed solution is filtered and concentrated by a membrane module. A second step in which the mixed solution in the microbial treatment tank is reduced by separating the liquid and the permeated liquid and discharging the permeated liquid in the membrane module to the outside; The third valve opens the fourth valve and the fifth valve, and the pump transfers all the concentrated liquid in the filtration treatment tank to the microbial treatment tank.
After closing all valves and washing the membrane module by pouring washing water into the filtration tank and blowing air through the air diffuser, open the second valve, the third valve, and the drain valve to release the washing water. A fourth step of discharging the water, a fifth step of closing all valves, putting a chemical solution into the filtration treatment tank to wash the membrane module with a chemical, and then adding a neutralizing agent into the chemical solution to neutralize the chemical solution. and a sixth step of restarting operation of the sewage treatment apparatus by opening the first valve, the second valve, and the fourth valve.
作用
上記本発明の構成において、運転中は,第1バルブ、第
2バルブおよび第4バルブが開かれており、ろ過処理槽
内の混合溶液は散気管から吹き出される曝気用空気の気
泡により上昇流となり、膜モジュールによりろ過処理さ
れて濃縮液と透過液とに分離される。濃縮液は、さらに
上昇して仕切壁越しに活性汚泥処理槽内に入り,檜内の
混合溶液と混合して下降し、第1連通管を経由してろ過
処理槽内にもどり、循環する。他方、膜モジュール内の
透過液は吸引ポンプにより外部に排出される。Effect In the configuration of the present invention described above, during operation, the first valve, the second valve, and the fourth valve are opened, and the mixed solution in the filtration treatment tank rises due to the bubbles of aeration air blown out from the aeration pipe. The resulting liquid is filtered by a membrane module and separated into a concentrated liquid and a permeated liquid. The concentrated liquid further rises, enters the activated sludge treatment tank over the partition wall, mixes with the mixed solution in the cypress, descends, returns to the filtration treatment tank via the first communication pipe, and circulates. On the other hand, the permeate inside the membrane module is discharged to the outside by a suction pump.
そして、膜モジュールを薬品洗浄する場合には、第1工
程で、汚水処理装置の運転を停止し、原水の供給も停止
する。第1バルブ、第2バルブおよび第3バルブ以外の
バルブをすべて閉じると、活性汚泥処理槽とろ過処理槽
とは第2連通管を介して連通される。第2工程で、ポン
プを運転して微生物処理槽内の混合溶液の一部をろ過処
理槽内に送りながら、混合溶液を膜モジュールによりろ
過処理して濃縮液と透過液とに分離し、膜モジュール内
の透過液を外部に排出すると、微生物処理槽内の混合溶
液は排出された透過液の量だけ減量する。第3工程で、
第1バルブおよび第3パルプを閉じるとともに、第2バ
ルブ、第4バルブおよび第5バルブを開くと、微生物処
理槽は遮断され、ろ過処理槽が第1連通管から第2連通
管を経由して移送管に連通される。そこで、ポンプを運
転すると、ろ過処理槽内に残留した濃縮液はすべて移送
管から微生物処理槽内に移送され、ろ過処理槽内は空に
なる。第4工程で、すべてのバルブを閉じ,ろ過処理槽
内に洗浄水を入れて散気管から空気を吹き込むと、洗浄
水はかくはんされて膜モジュールを水洗する。第2バル
ブ、第3バルブおよび排水バルブを開いて洗浄水を排出
後、第5工程で、すべてのバルブを閉じ、ろ過処理槽内
に薬液を入れて膜モジュールを薬品洗浄する。薬液は、
通常酸性であるので、後に運転を再開するとき、ろ過処
理槽内に薬液が残っていると、微生物が死滅するおそれ
がある。そこで、薬液中に中和剤を入れて薬液を中和さ
せ,微生物の死滅を防止する。When cleaning the membrane module with chemicals, in the first step, the operation of the sewage treatment equipment is stopped, and the supply of raw water is also stopped. When all valves other than the first valve, second valve, and third valve are closed, the activated sludge treatment tank and the filtration treatment tank are communicated via the second communication pipe. In the second step, while operating the pump to send a part of the mixed solution in the microbial treatment tank into the filtration treatment tank, the mixed solution is filtered by the membrane module and separated into a concentrated liquid and a permeated liquid. When the permeate in the module is discharged to the outside, the mixed solution in the microbial treatment tank is reduced by the amount of the discharged permeate. In the third step,
When the first valve and the third pulp are closed and the second valve, the fourth valve, and the fifth valve are opened, the microbial treatment tank is shut off and the filtration treatment tank is transferred from the first communication pipe to the second communication pipe. It communicates with the transfer pipe. Therefore, when the pump is operated, all the concentrated liquid remaining in the filtration tank is transferred from the transfer pipe to the microbial treatment tank, and the filtration tank becomes empty. In the fourth step, all valves are closed, cleaning water is poured into the filtration treatment tank, and air is blown through the aeration pipe, which agitates the cleaning water and washes the membrane module. After opening the second valve, third valve, and drain valve to discharge the cleaning water, in the fifth step, all the valves are closed and a chemical solution is poured into the filtration treatment tank to chemically clean the membrane module. The chemical solution is
Since it is usually acidic, if the chemical solution remains in the filtration treatment tank when restarting operation later, there is a risk that microorganisms will be killed. Therefore, a neutralizing agent is added to the chemical solution to neutralize the chemical solution and prevent the microorganisms from dying.
これで薬品洗浄が完了するので、第6工程で、第1バル
ブ、第2バルブおよび第4バルブを開き,汚水処理装置
の運転を再開するのである。ろ過処理槽内の中和水は、
微生物処理槽からの濃縮液と混合し、この濃縮液は元の
濃度にもどる。Since the chemical cleaning is now completed, in the sixth step, the first valve, the second valve, and the fourth valve are opened to restart the operation of the sewage treatment equipment. The neutralized water in the filtration treatment tank is
Mixed with the concentrate from the microbial treatment tank, this concentrate returns to its original concentration.
上記のように本発明の構成によれば、膜モジュールおよ
び活性汚泥のいずれをも外部に取り出すことなく薬品洗
浄g容易1=N,Lるうえに、汚水処理装置の運転休止
時間が短くてすむ。As described above, according to the configuration of the present invention, chemical cleaning is easy without taking out either the membrane module or the activated sludge to the outside, and the downtime of the sewage treatment equipment can be shortened. .
実施例 以下,本発明の一実施例を第1図に基づいて説明する。Example An embodiment of the present invention will be described below with reference to FIG.
本実施例における汚水処理装置は、第1図に示すように
活性汚泥処理槽11とろ過処理槽12とが仕切壁13を
介してこの仕切壁越しに連通可能に併設されてなるもの
である。活性汚泥処理槽11の底部には、第1バルブ1
4が接続されている。ろ過処理槽12は、内部に限外ろ
過膜を有する膜モジュール15が複数個設けられるとと
もに、膜モジュールの下方にブロワー16を有する曝気
用散気管17が設けられ、底部に第2バルブ18および
第3バルブ19が直列に接続されている。第1バルブ1
4には、第2バルブ18との間に第4バルブ20を有す
る第1連通管21と、第3バルブ19との間にポンブ2
2を有する第2連通管23とがそれぞれ接続されている
。第2連通管23のポンプ22と第3バルブ19との中
間には、第5バルブ24を有する移送管25と排水バル
ブ26を有する排水管27とがそれぞれ接続されている
。移送管25の他端は、活性汚泥処理槽11の上方に開
口している。28は原水供給管である。As shown in FIG. 1, the sewage treatment apparatus in this embodiment has an activated sludge treatment tank 11 and a filtration treatment tank 12 installed side by side through a partition wall 13 so as to be able to communicate with each other through the partition wall. At the bottom of the activated sludge treatment tank 11, a first valve 1 is installed.
4 are connected. The filtration treatment tank 12 is provided with a plurality of membrane modules 15 having ultrafiltration membranes therein, an aeration diffuser pipe 17 having a blower 16 below the membrane modules, and a second valve 18 and a second valve 18 at the bottom. Three valves 19 are connected in series. 1st valve 1
4, a first communication pipe 21 having a fourth valve 20 between it and the second valve 18 and a pump 2 between it and the third valve 19.
2 are connected to the second communication pipes 23 having the second communication pipes 23 and 23, respectively. A transfer pipe 25 having a fifth valve 24 and a drain pipe 27 having a drain valve 26 are connected to the second communication pipe 23 between the pump 22 and the third valve 19, respectively. The other end of the transfer pipe 25 opens above the activated sludge treatment tank 11. 28 is a raw water supply pipe.
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.
汚水処理装置の運転中は、第1バルブ14,第2バルブ
18および第4バルブ20を開いて、両槽11,12を
第1連通管21により連通しておく。汚水の原水29は
、原水供給管28から活性汚泥処理槽11内に供給され
て活性汚泥処理され、活性汚泥との混合溶液30となる
。この混合溶液30は、第1連通管21を経由してろ過
処理槽12内に入り、ブロヮー16により散気管17か
ら吹き出される曝気用空気31の気泡により上昇流とな
り、膜モジュール15によりろ過処理されて濃縮液と透
過液とに分離される。濃縮液は、さらに上昇し、仕切壁
13を越えて活性汚泥処理槽11内に入り、槽内の混合
溶液3oと混合して下降し、第1連通管21を経由して
ろ過処理槽12内にもどり,図中の矢印方向に循環する
。他方、膜モジュール15内の透過液は吸引ポンプ(図
示省略)により外部に排出される。During operation of the sewage treatment apparatus, the first valve 14, the second valve 18, and the fourth valve 20 are opened, and both tanks 11 and 12 are communicated through the first communication pipe 21. The raw water 29 of sewage is supplied from the raw water supply pipe 28 into the activated sludge treatment tank 11 and subjected to activated sludge treatment to become a mixed solution 30 with activated sludge. This mixed solution 30 enters the filtration treatment tank 12 via the first communication pipe 21, becomes an upward flow due to the bubbles of the aeration air 31 blown out from the diffuser pipe 17 by the blower 16, and is filtered by the membrane module 15. The liquid is separated into a concentrated liquid and a permeated liquid. The concentrated liquid further rises, crosses the partition wall 13 and enters the activated sludge treatment tank 11, mixes with the mixed solution 3o in the tank, descends, and enters the filtration treatment tank 12 via the first communication pipe 21. It returns and circulates in the direction of the arrow in the figure. On the other hand, the permeate in the membrane module 15 is discharged to the outside by a suction pump (not shown).
そして、膜モジュール15を薬品洗浄する場合には、第
1工程で、汚水処理装置の運転を停止し、原水29の供
給も停止する。第lバルブ14、第2バルブl8および
第3バルブ19を開き、他のバルブをすべて閉じると、
両槽11.. 12は第2連通管23を介して連通され
る。第2工程で、ポンブ22を運転して活性汚泥処理槽
11内の混合溶液30の一部をろ過処理槽12内に送り
ながら、混合溶液30を膜モジュール15によりろ過処
理して濃縮液と透過液とに分離し、膜モジュール15内
の透過液を吸引ポンプ(図示省略)により外部に排出す
ると,活性汚泥処理槽11内の混合溶液30は排出され
た透過液の量だけ減量する。この場合、幹−≠鈴i混合
溶液30の容量は、活性汚泥処理槽11内の混合液が仕
切壁13を越えることなくすべて槽11内に残留する程
度に留めておく。第3工程で、第lバルブ14および第
3バルブ19を閉じるとともに、第2バルブ18、第4
バルブ20および第5バルブ24を開くと、ろ過処理槽
12は、活性汚泥処理槽11から遮断され、第1連通管
21から第2連通管23を経由して移送管25に連通さ
れる。そこで、ポンプ22を運転すると、ろ過処理槽1
2内に残留した濃縮液はすべて移送管25から活性汚泥
処理槽11内に移送され、ろ過処理槽12内は空になる
。第4工程で、すべてのバルブを閉じ、ろ過処理槽12
内に洗浄水32を入れてブロワー16により散気管17
から空気31を吹き込むと、洗浄水32はかくはんされ
て膜モジュール15を水洗する。この場合、洗浄水32
の量は、空気31を吹き込まれても仕切壁13を越えな
い程度に留めておく。When cleaning the membrane module 15 with chemicals, in the first step, the operation of the sewage treatment device is stopped and the supply of raw water 29 is also stopped. When the first valve 14, the second valve l8 and the third valve 19 are opened and all other valves are closed,
Both tanks 11. .. 12 are communicated via a second communication pipe 23. In the second step, while operating the pump 22 to send a part of the mixed solution 30 in the activated sludge treatment tank 11 into the filtration treatment tank 12, the mixed solution 30 is filtered through the membrane module 15 and passed through the concentrated liquid. When the permeated liquid in the membrane module 15 is discharged to the outside by a suction pump (not shown), the mixed solution 30 in the activated sludge treatment tank 11 is reduced by the amount of the discharged permeated liquid. In this case, the volume of the trunk-≠bell i mixed solution 30 is kept to such an extent that all of the mixed liquid in the activated sludge treatment tank 11 remains in the tank 11 without exceeding the partition wall 13. In the third step, the first valve 14 and the third valve 19 are closed, and the second valve 18 and the fourth valve are closed.
When the valve 20 and the fifth valve 24 are opened, the filtration treatment tank 12 is cut off from the activated sludge treatment tank 11 and communicated with the transfer pipe 25 via the first communication pipe 21 and the second communication pipe 23. Therefore, when the pump 22 is operated, the filtration treatment tank 1
All the concentrated liquid remaining in the filter 2 is transferred from the transfer pipe 25 to the activated sludge treatment tank 11, and the filtration treatment tank 12 becomes empty. In the fourth step, all valves are closed and the filtration treatment tank 12
Cleaning water 32 is poured into the air diffuser pipe 17 using the blower 16.
When air 31 is blown into the washing water 32, the washing water 32 is stirred and the membrane module 15 is washed with water. In this case, the cleaning water 32
The amount of air 31 is kept to such an extent that it does not exceed the partition wall 13 even if the air 31 is blown.
水洗後,第2バルブ18、第3バルブ19および排水バ
ルブ26を開き、洗浄水32を排水管27から外部に排
出する。第5工程で、すべてのバルブを閉じ、ろ過処理
槽内にHC/などの薬液33を入れて膜モジュール15
を薬品洗浄する。この場合、薬液33の量は、薬液33
が仕切W13を越えないようにする。薬品洗浄後は,後
に運転を再開するとき、ろ過処理槽12内に薬液33が
残っていると活性汚泥中の微生物が死滅するおそれがあ
るので、薬液33中に中和剤を入れて中和させ、微生物
の死滅を防止する。After washing, the second valve 18, the third valve 19, and the drain valve 26 are opened, and the washing water 32 is discharged from the drain pipe 27 to the outside. In the fifth step, all valves are closed, and a chemical solution 33 such as HC/ is put into the filtration treatment tank, and the membrane module 15 is
Clean with chemicals. In this case, the amount of the chemical solution 33 is
prevent it from exceeding the partition W13. After chemical cleaning, when restarting operation later, if the chemical solution 33 remains in the filtration treatment tank 12, the microorganisms in the activated sludge may be killed, so a neutralizing agent is added to the chemical solution 33 to neutralize it. and prevent the death of microorganisms.
なお,上記薬品洗浄および中和の後、必要に応じて、N
aCIOなどの薬液によりさらに薬品洗浄し、その後中
和する場合もある。以上で薬品洗浄が完了するので、第
6工程で、第1バルブ14、第2バルブ18および第4
バルブ20を開いて両槽11.12を第1連通管21に
より連通させ、原水29を供給して汚水処理装置の運転
を再開するのである。ろ過処理槽12内に残留している
中和水34は、活性汚泥処理槽11からの濃縮液と混合
し,この濃縮液は元の濃度にもどる。In addition, after the above chemical cleaning and neutralization, N
In some cases, further chemical cleaning is performed using a chemical solution such as aCIO, followed by neutralization. Since the chemical cleaning is completed in the above steps, in the sixth step, the first valve 14, the second valve 18 and the fourth valve
The valve 20 is opened to communicate the two tanks 11 and 12 through the first communication pipe 21, raw water 29 is supplied, and the operation of the sewage treatment apparatus is restarted. The neutralized water 34 remaining in the filtration treatment tank 12 mixes with the concentrated liquid from the activated sludge treatment tank 11, and this concentrated liquid returns to its original concentration.
上記のように本実施例の構成によれば、膜モジュール1
5および活性汚泥のいずれをも外部に取り出すことなく
薬品洗浄できるので、洗浄が容易となるうえに、汚水処
理装置の運転休止時間が短くてすむのである。As described above, according to the configuration of this embodiment, the membrane module 1
5 and activated sludge can be cleaned with chemicals without taking them out to the outside, which not only makes cleaning easier, but also shortens the downtime of the sewage treatment equipment.
発明の効果
本発明は、以上説明したように、汚水処理装置の活性汚
泥処理槽とろ過処理槽とが仕切壁と第1および第2連通
管とにより連通・遮断可能に接続され、第2連通管に移
送管が接続され、膜モジュールを薬品洗浄するときには
、ろ過処理槽を活性汚泥処理槽から遮断し、すべての活
性汚泥を一時的に濃縮状態で活性汚泥処理槽内に貯留し
た後洗浄する構成としたので、膜モジュールおよび活性
汚泥のいずれをも外部に取り出すことなく薬品洗浄する
ことができる。したがって、薬品洗浄工程が容易化され
るだけでなく,薬品洗浄による汚水処理装置の運転休止
時間が短縮化されるという利点を有する。Effects of the Invention As explained above, in the present invention, an activated sludge treatment tank and a filtration treatment tank of a sewage treatment device are connected to each other so as to be able to communicate and shut off by a partition wall and first and second communication pipes, and the second communication A transfer pipe is connected to the pipe, and when cleaning the membrane module with chemicals, the filtration treatment tank is isolated from the activated sludge treatment tank, and all activated sludge is temporarily stored in the activated sludge treatment tank in a concentrated state before cleaning. With this configuration, chemical cleaning can be performed without taking out either the membrane module or the activated sludge to the outside. Therefore, there is an advantage that not only the chemical cleaning process is facilitated, but also the downtime of the sewage treatment equipment due to chemical cleaning is shortened.
第1図は本発明の一実施例を示す汚水処理装置の断面図
、第2図は従来の汚水処理装置の一例を示す断面図であ
る。
11・・・活性汚泥処理槽、12・・・ろ過処理槽、1
3・・・仕切壁、14・・・第1バルブ、15・・・膜
モジュール、17・・・散気管、18・・・第2バルブ
、19・・・第3バルブ、2o・・・第4バルブ、21
・・・第1連通管、22・・・ポンプ、23・・・第2
連通管、24・・・第5バルブ、25・・・移送管,2
6・・・排水バルブ.27・・・排水管、29・・・原
水、30・・・混合溶液、31・・・空気、32・・・
洗浄水、33・・・薬液。FIG. 1 is a sectional view of a sewage treatment apparatus according to an embodiment of the present invention, and FIG. 2 is a sectional view of an example of a conventional sewage treatment apparatus. 11... activated sludge treatment tank, 12... filtration treatment tank, 1
3... Partition wall, 14... First valve, 15... Membrane module, 17... Diffusion tube, 18... Second valve, 19... Third valve, 2o... Third valve 4 valves, 21
... first communication pipe, 22 ... pump, 23 ... second
Communication pipe, 24... Fifth valve, 25... Transfer pipe, 2
6... Drain valve. 27... Drain pipe, 29... Raw water, 30... Mixed solution, 31... Air, 32...
Washing water, 33...chemical solution.
Claims (1)
後の混合溶液をろ過膜を有する膜モジュールによりろ過
処理するろ過処理槽とを仕切壁を介して仕切壁越しに連
通可能に併設し、微生物処理槽の底部に第1バルブを接
続し、ろ過処理槽の内部に複数個の膜モジュールおよび
膜モジュールの下方の曝気用散気管を設け、前記ろ過処
理槽の底部に第2バルブおよび第3バルブを直列に接続
し、第1バルブに、第2バルブとの間に第4バルブを有
する第1連通管と、第3バルブとの間にポンプを有する
第2連通管とを接続し、第2連通管のポンプと第3バル
ブとの中間に、第5バルブを有する移送管と排水バルブ
を有する排水管とを接続し、移送管の他端を微生物処理
槽上に開口して汚水処理装置を構成するとともに、 微生物処理槽への原水の供給を停止し、かつ第1バルブ
、第2バルブおよび第3バルブ以外のバルブを閉じる第
1工程と、ポンプにより微生物処理槽内の混合溶液の一
部をろ過処理槽内に送りながら、混合溶液を膜モジュー
ルによりろ過処理して濃縮液と透過液とに分離し、膜モ
ジュール内の透過液を外部に排出することにより微生物
処理槽内の混合溶液を減量させる第2工程と、第1バル
ブおよび第3バルブを閉じるとともに、第2バルブ、第
4バルブおよび第5バルブを開き、ポンプによりろ過処
理槽内の濃縮液をすべて微生物処理槽内に移送する第3
工程と、すべてのバルブを閉じ、ろ過処理槽内に洗浄水
を入れて散気管から空気を吹き込むことにより膜モジュ
ールを水洗した後、第2バルブ、第3バルブおよび排水
バルブを開いて洗浄水を排出する第4工程と、すべての
バルブを閉じ、ろ過処理槽内に薬液を入れて膜モジュー
ルを薬品洗浄後、薬液中に中和剤を入れて薬液を中和さ
せる第5工程と、第1バルブ、第2バルブおよび第4バ
ルブを開いて汚水処理装置の運転を再開する第6工程と
を有することを特徴とする膜モジュールの薬品洗浄方法
。[Claims] 1. A microbial treatment tank that microbially treats raw water and a filtration tank that filters a mixed solution after microbial treatment using a membrane module having a filtration membrane are communicated through a partition wall. A first valve is connected to the bottom of the microbial treatment tank, a plurality of membrane modules and an aeration diffuser pipe below the membrane modules are provided inside the filtration treatment tank, and a first valve is connected to the bottom of the filtration treatment tank. The second valve and the third valve are connected in series, and the first valve has a first communicating pipe having a fourth valve between it and the second valve, and a second communicating pipe having a pump between the third valve. A transfer pipe having a fifth valve and a drain pipe having a drain valve are connected between the pump and the third valve of the second communication pipe, and the other end of the transfer pipe is opened above the microbial treatment tank. A first step of stopping the supply of raw water to the microbial treatment tank and closing valves other than the first valve, second valve, and third valve, and a pump to configure the sewage treatment equipment. While sending a part of the mixed solution into the filtration treatment tank, the mixed solution is filtered through a membrane module and separated into a concentrated liquid and a permeated liquid, and the permeated liquid in the membrane module is discharged to the outside for microbial treatment. The second step is to reduce the amount of mixed solution in the tank, close the first and third valves, open the second, fourth and fifth valves, and remove all the concentrated liquid in the filtration tank with microorganisms using a pump. The third to be transferred into the treatment tank
After closing all valves and washing the membrane module by pouring washing water into the filtration tank and blowing air through the air diffuser, open the second valve, the third valve, and the drain valve to release the washing water. A fourth step of discharging the water, a fifth step of closing all valves, putting a chemical solution into the filtration treatment tank to wash the membrane module with the chemical, and then adding a neutralizing agent into the chemical solution to neutralize the chemical solution; A method for cleaning a membrane module with chemicals, comprising: a sixth step of restarting operation of the sewage treatment equipment by opening the valve, the second valve, and the fourth valve.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1189798A JPH0722685B2 (en) | 1989-07-21 | 1989-07-21 | Membrane module chemical cleaning method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1189798A JPH0722685B2 (en) | 1989-07-21 | 1989-07-21 | Membrane module chemical cleaning method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0356192A true JPH0356192A (en) | 1991-03-11 |
JPH0722685B2 JPH0722685B2 (en) | 1995-03-15 |
Family
ID=16247391
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1189798A Expired - Fee Related JPH0722685B2 (en) | 1989-07-21 | 1989-07-21 | Membrane module chemical cleaning method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0722685B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04104895A (en) * | 1990-08-27 | 1992-04-07 | Ebara Infilco Co Ltd | Biological treating device for organic sewage |
JP2007196139A (en) * | 2006-01-26 | 2007-08-09 | Kobelco Eco-Solutions Co Ltd | Composite filter of media filter basin and membrane filter |
-
1989
- 1989-07-21 JP JP1189798A patent/JPH0722685B2/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04104895A (en) * | 1990-08-27 | 1992-04-07 | Ebara Infilco Co Ltd | Biological treating device for organic sewage |
JPH0683838B2 (en) * | 1990-08-27 | 1994-10-26 | 荏原インフイルコ株式会社 | Organic wastewater biological treatment equipment |
JP2007196139A (en) * | 2006-01-26 | 2007-08-09 | Kobelco Eco-Solutions Co Ltd | Composite filter of media filter basin and membrane filter |
Also Published As
Publication number | Publication date |
---|---|
JPH0722685B2 (en) | 1995-03-15 |
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