JPH08103603A - Upflow filtration method - Google Patents

Upflow filtration method

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Publication number
JPH08103603A
JPH08103603A JP6259684A JP25968494A JPH08103603A JP H08103603 A JPH08103603 A JP H08103603A JP 6259684 A JP6259684 A JP 6259684A JP 25968494 A JP25968494 A JP 25968494A JP H08103603 A JPH08103603 A JP H08103603A
Authority
JP
Japan
Prior art keywords
water
filter layer
washing
filtration
raw 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.)
Granted
Application number
JP6259684A
Other languages
Japanese (ja)
Other versions
JP3473132B2 (en
Inventor
Atsushi Watanabe
敦 渡辺
Hiroaki Ishida
浩昭 石田
Motoyuki Yoda
元之 依田
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries Ltd
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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP25968494A priority Critical patent/JP3473132B2/en
Publication of JPH08103603A publication Critical patent/JPH08103603A/en
Application granted granted Critical
Publication of JP3473132B2 publication Critical patent/JP3473132B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

(57)【要約】 【目的】 洗浄工程を終り、濾過工程を再開した当初に
得られる処理水中の濁質の濃度を低減する。 【構成】 処理槽1内に浮上濾材による濾層3を設け、
原水を濾層に上向流で通水して濾過工程を行い、洗浄水
を濾層に下向流で通水して洗浄工程を行う上向流濾過方
法において、処理槽に濾層上の水を槽底部に供給して循
環させる循環管9を設け、洗浄後に処理槽内の水を上記
循環管で循環させて濾層に上向流で所定時間通水し、そ
の後に原水を上向流で通水して濾過工程を行う。
(57) [Summary] [Purpose] To reduce the concentration of suspended matter in the treated water obtained at the beginning of the filtration process after the washing process. [Structure] A filter layer 3 of a floating filter medium is provided in the treatment tank 1,
In the up-flow filtration method, in which raw water is passed through the filter layer in an upward flow to perform the filtration step, and washing water is passed in a downward flow to perform the washing step, A circulation pipe 9 for supplying water to the bottom of the tank to circulate is provided, and after washing, the water in the treatment tank is circulated by the above circulation pipe to pass upward through the filter layer for a predetermined time, and then the raw water is raised. The filtration process is carried out by passing water in a stream.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、処理槽内に浮上濾材
による濾層を設けた上向流濾過装置の運転方法に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of operating an upflow filtration device having a filter layer of a floating filter material in a treatment tank.

【0002】[0002]

【従来の技術】ポリスチレン、ポリエチレン、ウレタン
樹脂等から球状、不定形状で、比重が1以下の浮上濾材
を発泡成形し、この浮上濾材を図1に示すように処理槽
1内のスクリーン2の下に投入し、浮上濾材をスクリー
ンの下に浮力で集結させて濾層3を構成し、原水を給水
管4、ポンプP1 で処理槽の底部に供給して槽内の濾層
中に上向流で通水し、原水中のSSを濾層に捕捉させ、
処理水を処理槽の上部の排水管5から排水して濾過工程
を行う上向流濾過装置は従来から公知である。又、濾層
を構成する浮上濾材の表面に微生物の生物膜を付着さ
せ、原水を濾層中に上向流で通水すると共に槽底の散気
管6から曝気して原水中のSSを濾層に捕捉させるばか
りでなく、原水が含有する溶存性有機物を微生物に分解
させて除去、低減する生物膜濾過も従来から公知であ
る。
2. Description of the Related Art A levitation filter medium having a spherical shape and an indefinite shape and a specific gravity of 1 or less is foam-molded from polystyrene, polyethylene, urethane resin or the like, and the levitation filter medium is placed under a screen 2 in a treatment tank 1 as shown in FIG. , The floating filter medium is collected under the screen by buoyancy to form the filter layer 3, and raw water is supplied to the bottom of the treatment tank by the water supply pipe 4 and the pump P1 to flow upward into the filter layer in the tank. To pass SS in the raw water to the filter layer,
An upflow filtration device that drains treated water from a drain pipe 5 at the upper part of a treatment tank to perform a filtration process has been conventionally known. In addition, a biofilm of microorganisms is attached to the surface of the flotation filter material that constitutes the filter layer, and raw water is passed through the filter layer in an upward flow and aeration is performed from the diffuser pipe 6 at the bottom of the tank to filter SS in the raw water. Biofilm filtration is known in the art, in which not only is it trapped in a layer, but also dissolved organic substances contained in raw water are decomposed into microorganisms to be removed and reduced.

【0003】濾過工程を継続すると捕捉したSSや、過
剰に成長した生物膜が浮上濾材同志の間隙を閉塞し、圧
力損失が高まってくる。圧力損失が所定の値に高まった
ら、給水管4の弁、排水管5の弁を閉じて濾過工程を中
断し、散水管7で洗浄水を濾層に上から供給すると共
に、槽底のドレン管8の弁を開き、ドレン管で槽内の水
を排出しながら下向流する洗浄水で浮上濾材を流動させ
る水洗浄と、ドレン管の弁を閉じ、洗浄水の供給を止
め、散気管6から空気を噴出し、気泡で浮上濾材を流動
させる空気洗浄を繰返して行うことにより浮上濾材から
SSや汚泥を剥離し、最後に洗浄水を散水管7から供給
し、ドレン管8の弁を開いてSSや汚泥をドレン管から
洗浄水と一緒に洗い出し、ドレン管から排出される洗浄
水にSSや汚泥が認められなくなったら散水管からの洗
浄水の供給を停め、ドレン管の弁を閉じ、洗浄工程を終
わる。洗浄水には濾過工程のときに排水管5から得た処
理水か、工業用水を使用する。
When the filtration process is continued, the trapped SS and the excessively grown biofilm block the gap between the floating filter media and the pressure loss increases. When the pressure loss increases to a predetermined value, the valve of the water supply pipe 4 and the valve of the drainage pipe 5 are closed to interrupt the filtration process, and the sprinkling pipe 7 supplies the wash water to the filter layer from above and the drain at the bottom of the tank. The valve of the pipe 8 is opened, the drain pipe discharges the water in the tank and the washing water flowing downward causes the floating filter medium to flow, and the valve of the drain pipe is closed to stop the supply of the washing water, and the diffuser pipe. By ejecting air from 6 and repeating air washing in which the floating filter medium is caused to flow by air bubbles, SS and sludge are separated from the floating filter medium, and finally washing water is supplied from the sprinkler pipe 7 and the valve of the drain pipe 8 is turned on. Open to wash out SS and sludge from the drain pipe together with the wash water, and when SS and sludge are no longer observed in the wash water discharged from the drain pipe, stop the supply of wash water from the sprinkler pipe and close the drain pipe valve. , The washing process is completed. As the wash water, treated water obtained from the drainage pipe 5 at the time of the filtration step or industrial water is used.

【0004】[0004]

【発明が解決しようとする課題】上記のようにして洗浄
工程を終り、原水を給水管4、ポンプP1 で処理槽の底
部に供給し、槽内の濾層3中に上向流で通水する濾過工
程を再開すると、濾過工程の当初に排水管5に得られる
処理水中にSSや汚泥が混ざって排出される。これは、
洗浄工程の際の洗浄水は濾層中を下向流するのに対し、
濾過工程の際の原水は濾層中を逆に上向流するため、洗
浄直後の濾過工程の原水の上向流通水で濾層が圧密化す
るまでの間、浮上性濾材が乱され、濾層中に存在する少
量のSSや汚泥が処理水に混ざって排出されるのであ
る。このため、濾過工程を開始した当初の一定時間、排
水管5に排出される処理水を原水の水槽に返送し、その
後、SSや汚泥が混ざらない処理水を得るようにしてい
る。しかし、そうすると、原水の水槽を大型にする必要
がある。
After the cleaning process is completed as described above, raw water is supplied to the bottom of the treatment tank by the water supply pipe 4 and the pump P1, and the water is passed upward through the filter bed 3 in the tank. When the filtration step is restarted, SS and sludge are mixed and discharged into the treated water obtained in the drain pipe 5 at the beginning of the filtration step. this is,
While the washing water during the washing step flows downward in the filter layer,
Since the raw water in the filtration step flows upward in the filter layer in the reverse direction, the buoyant filter medium is disturbed until the filter layer is consolidated by the upward flowing water of the raw water in the filtration step immediately after washing. A small amount of SS and sludge existing in the bed is mixed with the treated water and discharged. For this reason, the treated water discharged to the drainage pipe 5 is returned to the raw water tank for a certain period of time at the beginning of the filtration step, and thereafter, treated water in which SS and sludge are not mixed is obtained. However, if so, it is necessary to make the tank for raw water large.

【0005】[0005]

【課題を解決するための手段】本発明は上述した問題点
を解消することを目的に開発されたのであって、処理槽
に濾層上の水を槽底部に供給して循環させる循環管を設
け、洗浄後に処理槽内の水を上記循環管で循環させて濾
層に上向流で所定時間通水し、その後に原水を上向流で
通水して濾過工程を行うことを特徴とする。
The present invention was developed for the purpose of solving the above-mentioned problems, and a circulation pipe for supplying water on the filter layer to the bottom of the tank and circulating it in the treatment tank is provided. After the cleaning, the water in the treatment tank is circulated through the circulation pipe after washing and is passed through the filter layer in an upward flow for a predetermined time, and then raw water is passed in an upward flow to perform a filtration step. To do.

【0006】[0006]

【実施例】処理槽1に、濾層3の上部の水を槽底部に循
環させる循環ポンプP2 を有する循環管9を設ける。そ
して洗浄工程が終ったら濾過工程を再開する前に循環ポ
ンプP2 を運転し、処理槽内の濾層上の水を循環管9で
槽底部に供給し、濾層中を上向流で通水して循環させ
る。これにより、循環の当初、浮上濾材は流動するが、
やがて浮上濾材はスクリーン2の下に浮力でギッシリと
密集して濾層は圧密化し、循環する水に含まれていたS
Sや汚泥は圧密化した濾層に捕捉されて循環する水の中
に存在しなくなる。
EXAMPLE The treatment tank 1 is provided with a circulation pipe 9 having a circulation pump P2 for circulating the water above the filter layer 3 to the bottom of the tank. Then, after the washing step is completed, the circulation pump P2 is operated before the filtration step is restarted, and the water on the filter layer in the treatment tank is supplied to the bottom of the tank through the circulation pipe 9 so that water flows upward in the filter layer. And circulate. As a result, at the beginning of circulation, the floating filter medium flows,
Eventually, the levitation filter material was tightly gathered under the screen 2 due to buoyancy and the filter layer was consolidated, and S contained in the circulating water was added.
S and sludge are captured by the compacted filter bed and are not present in the circulating water.

【0007】必要ならば処理槽には濾層の上部に水の濁
度を検出する濁質濃度検出器10を設け、濾層の上部の
水にSSや汚泥が存在しないことを検出したら、循環ポ
ンプP2 を停め、循環管の弁を閉じて循環工程を止め、
給水管と排水管の弁を開き、ポンプP1 を運転して濾過
工程を再開する。これによりSSや汚泥を含むことが少
ない処理水を得ることができる。
If necessary, the treatment tank is provided with a turbidity concentration detector 10 for detecting the turbidity of water above the filter layer, and if it is detected that SS or sludge is not present in the water above the filter layer, it is circulated. Stop the pump P2, close the valve of the circulation pipe, stop the circulation process,
The valves of the water supply pipe and the drainage pipe are opened, and the pump P1 is operated to restart the filtration process. As a result, treated water containing less SS and sludge can be obtained.

【0008】直径400mm、高さ5200mmの処理
槽を使用した図1の生物膜濾過装置により硝化脱窒運転
を行った。浮上濾材には粒径3.5mm、比重0.03
の発泡ポリスチレン製のものを使用し、濾層の高さは3
000mmにした。窒素の除去は濾層の上部の処理水の
一部を原水に循環して脱窒を行う循環法を採用した。原
水にはNH4 −N=50mg/立、BOD170mg/
立、SS=8mg/立の産業排水を用いた。
Nitrification and denitrification operation was performed by the biofilm filtration apparatus of FIG. 1 using a treatment tank having a diameter of 400 mm and a height of 5200 mm. Floating filter media has a particle size of 3.5 mm and a specific gravity of 0.03
Made of expanded polystyrene, and the height of the filter layer is 3
000 mm. Nitrogen was removed by a circulation method in which part of the treated water in the upper part of the filter bed was circulated to the raw water for denitrification. In raw water, NH 4 -N = 50 mg / stand, BOD 170 mg /
Vertical, SS = 8 mg / vertical industrial wastewater was used.

【0009】洗浄後、すぐに原水を上向流で濾層に通水
して濾過工程を行う試験(従来法)と、洗浄工程後、1
0分間原水を通水しないで循環工程を行い、それから原
水を上向流で濾層に通水して濾過工程を行う試験(本発
明方法)を行った。濾過工程での原水の上向流通水LV
はいずれも4m/時であった。尚、本発明方法の循環工
程での上向流通水LVは、濾層を早く圧密化し、SSや
汚泥の捕捉を早めるため10m/時にした。試験の結果
は図2に示す通りで、従来法では原水の通水を開始して
5分後の処理水のSS濃度は約50mg/立、その後は
SS濃度は低減したが通水開始20分後の処理水のSS
濃度はまだ10mg/立であった。これに対して本発明
方法では原水の通水を開始して5分後の処理水のSS濃
度は10mg/立、その後はSS濃度は低減し、通水開
始20分後の処理水のSS濃度は5mg/立であり、従
来法に較べて遥かに低かった。
A test (conventional method) in which raw water is immediately passed through the filter layer in an upward flow after washing to carry out a filtering step, and after the washing step, 1
A test (the method of the present invention) was conducted in which the circulation step was carried out for 0 minutes without passing the raw water, and then the raw water was passed through the filter layer in an upward flow to perform the filtration step. Upward circulation water LV of raw water in the filtration process
Was 4 m / hour. The upward flowing water LV in the circulation step of the method of the present invention was 10 m / hour in order to quickly consolidate the filter layer and accelerate the capture of SS and sludge. The results of the test are shown in Fig. 2, and in the conventional method, the SS concentration of the treated water 5 minutes after starting the passage of the raw water was about 50 mg / stand, and after that, the SS concentration was reduced, but 20 minutes after the passage of water. Later treated water SS
The concentration was still 10 mg / cubic. On the other hand, in the method of the present invention, the SS concentration of the treated water 5 minutes after starting the passage of the raw water is 10 mg / stand, and the SS concentration decreases thereafter, and the SS concentration of the treated water 20 minutes after the start of the passage of water. Was 5 mg / stand, which was far lower than that of the conventional method.

【0010】[0010]

【発明の効果】以上で明らかなように、本発明によれ
ば、浮上濾材に生物膜を付着した生物膜濾過でも浮上濾
材に生物膜を付着しない単純濾過でも洗浄工程を行った
のち濾過工程を再開したとき、SSや汚泥を含むことが
非常に少ない処理水を得ることができる。従って濾過工
程を再開した当初の処理水を原水の貯槽に戻さなくても
よいので、貯槽を大型化する必要がない。
As is apparent from the above, according to the present invention, the washing step is performed after the washing step is performed by the biofilm filtration in which the biofilm is attached to the flotation filter or the simple filtration in which the biofilm is not attached to the flotation filter. When restarted, treated water containing very little SS and sludge can be obtained. Therefore, it is not necessary to return the treated water at the beginning of the filtration process to the raw water storage tank, and there is no need to upsize the storage tank.

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

【図1】本発明の濾過方法を行うことができる上向流濾
過装置の断面図である。
FIG. 1 is a cross-sectional view of an upflow filtration device that can perform the filtration method of the present invention.

【図2】従来法の濾過と、本発明の方法の濾過を行った
場合の処理水中の濁度濃度の経時変化を示すグラフであ
る。
FIG. 2 is a graph showing changes over time in the turbidity concentration in treated water when the filtration according to the conventional method and the filtration according to the method of the present invention are performed.

【符号の説明】[Explanation of symbols]

1 処理槽 2 スクリーン 3 浮上濾材による濾層 4 原水の給水管 5 処理水の排水管 6 散気管 7 洗浄水の散水管 8 ドレン管 9 循環管 10 濁度濃度検出器 P1 原水供給ポンプ P2 循環ポンプ 1 Treatment tank 2 Screen 3 Filter layer by floating filter material 4 Raw water supply pipe 5 Treated water drain pipe 6 Diffuser pipe 7 Wash water sprinkler pipe 8 Drain pipe 9 Circulation pipe 10 Turbidity concentration detector P1 Raw water supply pump P2 Circulation pump

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 処理槽内に浮上濾材による濾層を設け、
原水を濾層に上向流で通水して濾過工程を行い、洗浄水
を濾層に下向流で通水して洗浄工程を行う上向流濾過方
法において、処理槽に濾層上の水を槽底部に供給して循
環させる循環管を設け、洗浄後に処理槽内の水を上記循
環管で循環させて濾層に上向流で所定時間通水し、その
後に原水を上向流で通水して濾過工程を行うことを特徴
とする上向流濾過方法。
1. A filter layer comprising a floating filter material is provided in a treatment tank,
In the up-flow filtration method, in which raw water is passed through the filter layer in an upward flow to perform the filtration step, and washing water is passed in a downward flow to perform the washing step, A circulation pipe for supplying water to the bottom of the tank to circulate is provided, and after washing, the water in the treatment tank is circulated by the above circulation pipe to flow upward through the filter layer for a predetermined time, and then the raw water flows upward. An upflow filtration method, characterized in that the filtration step is carried out by passing water through.
JP25968494A 1994-09-30 1994-09-30 Upflow filtration method Expired - Fee Related JP3473132B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25968494A JP3473132B2 (en) 1994-09-30 1994-09-30 Upflow filtration method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25968494A JP3473132B2 (en) 1994-09-30 1994-09-30 Upflow filtration method

Publications (2)

Publication Number Publication Date
JPH08103603A true JPH08103603A (en) 1996-04-23
JP3473132B2 JP3473132B2 (en) 2003-12-02

Family

ID=17337483

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25968494A Expired - Fee Related JP3473132B2 (en) 1994-09-30 1994-09-30 Upflow filtration method

Country Status (1)

Country Link
JP (1) JP3473132B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000051615A (en) * 1998-08-11 2000-02-22 Meidensha Corp Apparatus and method for controlling washing of filtration pond
KR100864642B1 (en) * 2008-05-23 2008-10-23 유네코개발 주식회사 Upflow expanded bed activated carbon adsorption filtration device and cleaning method thereof
JP2009090227A (en) * 2007-10-10 2009-04-30 Japan Organo Co Ltd Aggregation filtration treatment method and aggregation filtration treatment apparatus
JP2012035238A (en) * 2010-08-11 2012-02-23 Sankyo Giken Kogyo Kk Solid-liquid separation method and solid-liquid separation device
JP2021094514A (en) * 2019-12-16 2021-06-24 メタウォーター株式会社 Filtration device and cleaning method for filtration device

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5326861B2 (en) 2009-06-26 2013-10-30 Dic株式会社 Curable resin composition, cured product thereof, printed wiring board

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000051615A (en) * 1998-08-11 2000-02-22 Meidensha Corp Apparatus and method for controlling washing of filtration pond
JP2009090227A (en) * 2007-10-10 2009-04-30 Japan Organo Co Ltd Aggregation filtration treatment method and aggregation filtration treatment apparatus
KR100864642B1 (en) * 2008-05-23 2008-10-23 유네코개발 주식회사 Upflow expanded bed activated carbon adsorption filtration device and cleaning method thereof
JP2012035238A (en) * 2010-08-11 2012-02-23 Sankyo Giken Kogyo Kk Solid-liquid separation method and solid-liquid separation device
JP2021094514A (en) * 2019-12-16 2021-06-24 メタウォーター株式会社 Filtration device and cleaning method for filtration device

Also Published As

Publication number Publication date
JP3473132B2 (en) 2003-12-02

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