JPH1147511A - Filtration pond and method for operation thereof - Google Patents

Filtration pond and method for operation thereof

Info

Publication number
JPH1147511A
JPH1147511A JP9202822A JP20282297A JPH1147511A JP H1147511 A JPH1147511 A JP H1147511A JP 9202822 A JP9202822 A JP 9202822A JP 20282297 A JP20282297 A JP 20282297A JP H1147511 A JPH1147511 A JP H1147511A
Authority
JP
Japan
Prior art keywords
water
filtration
turbidity
drainage
drain
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.)
Pending
Application number
JP9202822A
Other languages
Japanese (ja)
Inventor
Kawamura Susumu
カワムラ ススム
Naokatsu Tanabe
直勝 田名部
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.)
Maezawa Industries Inc
Original Assignee
Maezawa Industries Inc
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 Maezawa Industries Inc filed Critical Maezawa Industries Inc
Priority to JP9202822A priority Critical patent/JPH1147511A/en
Publication of JPH1147511A publication Critical patent/JPH1147511A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To improve water recovery ratio in a water purification facility by reusing discharged water and to keep the turbidity of water at the outlet of a filtration pond 0.1 degree or lower by smoothly switching the filtration operation from water discharging operation. SOLUTION: On completion of the back washing operation of a filtration pond A, a water discharge valve 6a is opened and a water discharge pump 9 is started and while the turbidity of the discharged water is measured by a turbidity meter 11, the flow rate of the water discharge pump 9 is gradually increased and when the turbidity of the discharged water is lowered to a set turbidity or lower and the filtration speed reaches a set speed, the water discharge operation is completed and then a flow out valve 3a is opened and the water discharge valve 6a is closed to shift to the normal filtration operation.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、ろ過池及びその運
転方法に関し、詳しくは、浄水場に設けられている急速
ろ過池における捨水操作に関するものであり、既設及び
新設のいずれにも適用できるろ過池及びその運転方法に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter pond and a method for operating the filter, and more particularly, to a drainage operation in a rapid filter pond provided in a water purification plant, and can be applied to both existing and new filters. The present invention relates to a filter pond and its operation method.

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】浄水場
での浄水処理においては、クリプトスポリジウム対策と
して、ろ過池出口の水の濁度を常時把握し、ろ過池出口
の濁度を0.1度以下に維持するようにしている。した
がって、ろ過池の洗浄等の操作を行った後は、ろ過機能
が発現していないため、ろ過池出口の濁度が0.1度以
下になるまで捨水を行うようにしている。しかし、この
捨水操作は、30分程度の時間を要するだけでなく、こ
の間は大量の水を無駄に捨てることになる。また、捨水
操作から通常のろ過運転に切換えた際にろ過速度が急激
に上昇すると、濁度も上昇するため、ろ過池出口の濁度
を0.1度以下に維持することが困難となる。
2. Description of the Related Art In water purification treatment at a water purification plant, as a measure against Cryptosporidium, the turbidity of water at the outlet of a filtration pond is constantly monitored, and the turbidity of the outlet of the filtration pond is reduced to 0.1. Degree below. Therefore, after performing operations such as washing of the filtration pond, since the filtration function is not developed, water is drained until the turbidity at the outlet of the filtration pond becomes 0.1 ° or less. However, this draining operation not only takes about 30 minutes, but also wastes a large amount of water during this time. In addition, when the filtration speed is rapidly increased when the operation is switched from the waste water operation to the normal filtration operation, the turbidity also increases, so that it is difficult to maintain the turbidity at the outlet of the filtration tank at 0.1 degrees or less. .

【0003】そこで本発明は、捨水を再利用することに
よって浄水場での水回収率を向上させ、水資源の有効利
用が図れるとともに、捨水操作からろ過運転への切換え
も円滑に行うことができ、ろ過池出口の水の濁度を0.
1度以下に確実に維持することができるろ過池及びその
運転方法を提供することを目的としている。
[0003] Accordingly, the present invention is to improve the water recovery rate in a water purification plant by reusing waste water, to achieve effective use of water resources, and to smoothly switch from waste water operation to filtration operation. And the turbidity of the water at the outlet of the filtration pond is reduced to 0.
It is an object of the present invention to provide a filter pond that can be reliably maintained at a temperature of once or less and a method of operating the filter.

【0004】[0004]

【課題を解決するための手段】上記目的を達成するた
め、本発明のろ過池は、原水渠と、該原水渠にそれぞれ
流入弁を介して接続した複数のろ過池と、該ろ過池にそ
れぞれ流出弁を介して接続した浄水池と、各ろ過池から
の逆洗排水を排出するそれぞれの排水弁と、各ろ過池に
それぞれ捨水弁を介して接続した捨水管と、各捨水管を
合流して捨水を前記原水渠に戻す集合捨水管と、該集合
捨水管に設けられた捨水ポンプ,流量計及び濁度計とを
備えていることを特徴としている。
In order to achieve the above object, a filtration pond according to the present invention comprises a raw culvert, a plurality of filtration ponds connected to the raw culvert via respective inflow valves, and Merges the water purifier connected via the outflow valve, each drain valve discharging backwash drainage from each filter pond, the drainage pipe connected to each filter pond via the drainage valve, and each drainage pipe It is characterized by comprising a collecting drain pipe for returning the waste water to the raw sewer, and a drain pump, a flow meter and a turbidity meter provided in the collecting drain pipe.

【0005】また、本発明のろ過池の運転方法は、上記
構成のろ過池の運転方法、特に捨水操作時の運転方法で
あって、ろ過池の逆洗操作終了後、前記捨水弁を開いて
捨水ポンプを作動させ、前記濁度計で捨水の濁度を測定
しながら捨水ポンプの流量を徐々に増加させ、捨水の濁
度が設定濁度以下となり、ろ過速度が設定速度になった
ときに捨水操作を終了し、前記流出弁を開いて捨水弁を
閉じ、通常のろ過運転に移行することを特徴とし、さら
に、前記捨水操作の開始時に、捨水の濁度が所定値を超
えるときには、該捨水を集合捨水管から原水渠に戻すこ
となく、原水渠入口前から分岐した捨水排出管を介して
捨水貯槽に排出することを特徴としている。
[0005] The method of operating a filter pond of the present invention is a method of operating the filter pond having the above-described structure, particularly an operation method of drainage operation. Open and operate the wastewater pump, gradually increase the flow rate of the wastewater pump while measuring the turbidity of the wastewater with the turbidity meter, the turbidity of the wastewater becomes less than the set turbidity, and the filtration speed is set. When the speed reaches the speed, the drainage operation is terminated, the outflow valve is opened, the drainage valve is closed, and a transition is made to a normal filtration operation, and further, at the start of the drainage operation, the drainage operation is performed. When the turbidity exceeds a predetermined value, the wastewater is discharged to a wastewater storage tank via a wastewater discharge pipe branched from the entrance of the raw sewer without returning the wastewater from the collective drainage pipe to the raw sewer.

【0006】[0006]

【発明の実施の形態】図1は本発明のろ過池の一形態例
を示す系統図であって、4つのろ過池A,B,C,Dを
備えたものである。このろ過池は、原水渠1と、該原水
渠1にそれぞれ流入弁2a,2b,2c,2dを介して
接続したろ過池A,B,C,Dと、該ろ過池A,B,
C,Dにそれぞれ流出弁3a,3b,3c,3dを介し
て接続した浄水池4と、各ろ過池A,B,C,Dからの
逆洗排水を排出するそれぞれの排水弁5a,5b,5
c,5dと、各ろ過池A,B,C,Dにそれぞれ捨水弁
6a,6b,6c,6dを介して接続した捨水管7a,
7b,7c,7dと、各捨水管7a,7b,7c,7d
を合流して捨水を前記原水渠1に戻す集合捨水管8と、
該集合捨水管8に設けられた捨水ポンプ9,捨水流量計
10及び濁度計11とを備えている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a system diagram showing one embodiment of a filter pond according to the present invention, which comprises four filter ponds A, B, C and D. The filter ponds are raw water culverts 1, filter ponds A, B, C, and D connected to the raw water culverts 1 through inlet valves 2a, 2b, 2c, and 2d, respectively.
Water purification tank 4 connected to C and D through outflow valves 3a, 3b, 3c and 3d, respectively, and drain valves 5a, 5b and 5b for discharging backwash wastewater from each of filtration ponds A, B, C and D. 5
c, 5d, and a drainage pipe 7a connected to each of the filtration ponds A, B, C, D via drainage valves 6a, 6b, 6c, 6d, respectively.
7b, 7c, 7d and each drainage pipe 7a, 7b, 7c, 7d
And a collecting drain pipe 8 for returning the waste water to the raw culvert 1;
A water pump 9, a water flow meter 10, and a turbidity meter 11 are provided in the collecting water pipe 8.

【0007】前記流出弁3a,3b,3c,3dにはモ
ーターMで開閉される流量調整弁が用いられており、各
弁と直列に設けられたろ過流量計12a,12b,12
c,12dによって各ろ過池A,B,C,Dが適正なろ
過水量になるように調節される。また、捨水ポンプ9に
は回転数の制御によって流量調節を行える形式のものが
用いられており、前記捨水流量計10によって適正な流
量に制御される。
As the outflow valves 3a, 3b, 3c, 3d, flow regulating valves which are opened and closed by a motor M are used, and filtration flow meters 12a, 12b, 12 provided in series with the respective valves.
Each of the filtration ponds A, B, C, and D is adjusted by c and 12d so as to have an appropriate amount of filtered water. Also, a pump that can adjust the flow rate by controlling the number of rotations is used as the water drainage pump 9, and the flow rate is controlled by the water drainage flow meter 10 to an appropriate flow rate.

【0008】さらに、前記集合捨水管8には、捨水中の
微粒子を測定する微粒子計測計(図示せず)に接続する
サンプリング管13及びサンプリング弁14と、集合捨
水管8の捨水を必要に応じて洗浄排水貯槽(図示せず)
に排出するための捨水排出管15と、この捨水排出管1
5への捨水の排出を切換えるための切換弁16,17
と、原水(未ろ過水)がろ過水側へ逆流することを防止
するためのエアギャップ18とが設けられている。
Further, the collecting drainage pipe 8 needs a sampling pipe 13 and a sampling valve 14 connected to a particle measuring instrument (not shown) for measuring fine particles in the wastewater, and requires drainage of the collecting drainage pipe 8. Washing drainage storage tank (not shown)
Drainage pipe 15 for discharging water to the drain and this wastewater discharge pipe 1
Switching valves 16 and 17 for switching the discharge of waste water to
And an air gap 18 for preventing the raw water (unfiltered water) from flowing back to the filtered water side.

【0009】通常のろ過運転では、原水は、原水渠1か
ら流入弁2a〜2dを通ってろ過池A〜Dに供給され、
各ろ過池A〜Dでろ過処理された浄水は、ろ過流量計1
2a〜12dによって流量制御された流出弁3a〜3d
を通って浄水池4に流入する。
In a normal filtration operation, raw water is supplied from raw culvert 1 to filtration ponds A to D through inlet valves 2a to 2d.
The purified water filtered in each of the filtration ponds A to D is supplied to the filtration flow meter 1
Outflow valves 3a to 3d whose flow rates are controlled by 2a to 12d
And flows into the water purification tank 4.

【0010】ろ過池の逆洗は、各ろ過池について順次行
われ、例えば、ろ過池Aの逆洗及び捨水操作を終えた
後、ろ過池Bが逆洗及び捨水操作に入り、その後、ろ過
池C,Dの逆洗操作を順次行うように設定されている。
[0010] The backwashing of the filtration basin is performed sequentially for each filtration basin. For example, after the backwashing and the drainage operation of the filtration basin A are completed, the filtration basin B starts the backwashing and the drainage operation. It is set so that the backwash operation of the filtration ponds C and D is performed sequentially.

【0011】ここで、ろ過池Aがろ過運転から逆洗操作
に入った状態から、上記ろ過池の運転方法を説明する。
まず、流入弁2aを閉じて原水の流入を遮断する。この
とき、流出弁3aは開、排水弁5a及び捨水弁6aは
閉、捨水ポンプ9は停止中である。逆洗の操作は、ろ過
池の形式によって異なるが、通常は、流出弁3aを閉
じ、排水弁5aを開いてろ過池A内の水(洗浄排水)を
洗浄排水貯槽に排出し、浄水池4内の浄水を洗浄水とし
てろ過池Aに逆流させることにより行われる。
Here, a method of operating the filter pond from the state in which the filter pond A has entered the backwashing operation from the filter operation will be described.
First, the inflow valve 2a is closed to shut off the inflow of raw water. At this time, the outflow valve 3a is open, the drain valve 5a and the drain valve 6a are closed, and the drain pump 9 is stopped. The backwashing operation varies depending on the type of the filtration pond. Usually, the outflow valve 3a is closed and the drainage valve 5a is opened to discharge the water (washing wastewater) in the filtration pond A to the washing drainage storage tank. This is performed by flowing back the purified water in the filter A as the washing water.

【0012】逆洗操作が終了したら捨水操作に入り、流
出弁3a及び排水弁5aを閉じ状態として流入弁2a及
び捨水弁6aを開き、捨水ポンプ9を始動する。このと
き、操作開始時から捨水を切換弁16,エアギャップ1
8を介して原水渠1に戻すようにしてもよいが、捨水の
濁度が高い場合、例えば、濁度が1度を超える場合は、
集合捨水管8の切換弁16を閉じ、捨水排出管15の切
換弁17を開いて捨水を洗浄排水貯槽に排出するように
してもよい。
When the backwashing operation is completed, the drainage operation is started, the outflow valve 3a and the drainage valve 5a are closed, the inflow valve 2a and the drainage valve 6a are opened, and the drainage pump 9 is started. At this time, the water is discarded from the start of the operation by switching the switching valve 16
Although it may be returned to the raw culvert 1 via 8, when the turbidity of the waste water is high, for example, when the turbidity exceeds 1 degree,
The switching valve 16 of the collecting drain pipe 8 may be closed, and the switching valve 17 of the drain pipe 15 may be opened to discharge the waste water to the washing and drainage storage tank.

【0013】捨水ポンプ9の回転数は、操作開始時は低
速とし、徐々に回転数を上げて捨水量を増加させ、捨水
時のろ過速度を徐々に上昇させて最終的には通常のろ過
運転時のろ過速度と同じ速度にする。この捨水ポンプ9
の制御は、濁度計11で計測した濁度に応じて行うこと
もでき、濁度が高い場合には低速とし、濁度の低下に伴
って増速するようにしてもよい。
The rotation speed of the water drainage pump 9 is set to a low speed at the start of operation, the rotation speed is gradually increased to increase the amount of water drainage, and the filtration speed at the time of water drainage is gradually increased. Set the same filtration speed as the filtration speed. This waste water pump 9
Can be performed according to the turbidity measured by the turbidity meter 11, and when the turbidity is high, the speed may be set to a low speed, and the speed may be increased as the turbidity decreases.

【0014】そして、濁度計11で計測した濁度あるい
は微粒子計測計の測定値があらかじめ設定された設定値
となり、ろ過速度が通常のろ過運転時のろ過速度と同じ
速度になったら流出弁3aを開き、捨水ポンプ9を停止
させるとともに捨水弁6aを閉じ、捨水操作からろ過運
転に移行する。次いで、他のろ過池における逆洗及び捨
水操作が同様にして順次行われる。
When the turbidity measured by the turbidimeter 11 or the value measured by the fine particle meter becomes a preset value, and the filtration speed becomes the same as the filtration speed in the ordinary filtration operation, the outflow valve 3a Is opened, the drainage pump 9 is stopped, the drainage valve 6a is closed, and the operation shifts from the drainage operation to the filtration operation. Next, backwashing and drainage operations in other filtration ponds are performed sequentially in the same manner.

【0015】上述のようにして捨水操作を行うことによ
り、浄水場での水回収率を向上できるとともに、ろ過水
の濁度を確実に0.1度以下に維持することができる。
すなわち、捨水操作において、従来は洗浄排水貯槽に排
出していた捨水を捨水ポンプ9によって原水渠1に戻し
ており、また、濁度が高い捨水を捨水排出管15から洗
浄排水貯槽に排出したとしても、従来に比べて極めて少
量であり、逆洗操作時の洗浄排水と僅かな捨水を排出す
るだけで流入原水の大部分を浄化水として供給すること
ができる。これにより、水資源の有効利用、渇水対策に
効果的である。
By performing the water draining operation as described above, the water recovery rate at the water purification plant can be improved, and the turbidity of the filtered water can be reliably maintained at 0.1 degrees or less.
That is, in the drainage operation, the drainage water that was conventionally discharged to the cleaning drainage storage tank is returned to the raw culvert 1 by the drainage pump 9, and the water with high turbidity is washed and drained from the drainage discharge pipe 15. Even if it is discharged to a storage tank, the amount is extremely small compared to the conventional one, and most of the inflowing raw water can be supplied as purified water only by discharging the washing wastewater and a small amount of wastewater during the backwashing operation. This is effective for effective use of water resources and measures against drought.

【0016】また、捨水ポンプ9によって捨水時のろ過
速度がろ過運転時のろ過速度と同じ速度になった状態
で、捨水操作からろ過運転に切換えるので、ろ過速度の
急変による濁度の上昇が防止でき、ろ過池出口の濁度を
0.1度以下に確実に維持することができる。
In addition, since the drainage operation is switched from the drainage operation to the filtration operation in a state where the filtration speed at the time of the water drainage is equal to the filtration speed at the time of the filtration operation, the turbidity due to the sudden change of the filtration speed is reduced. The rise can be prevented, and the turbidity at the outlet of the filtration pond can be reliably maintained at 0.1 ° or less.

【0017】さらに、集合捨水管8に濁度計11を設置
するだけで必要十分な濁度管理を行うことができるた
め、各ろ過池からの捨水管に濁度計をそれぞれ設ける必
要がなくなる。
Furthermore, since the turbidity meter 11 can be installed in the collecting drain pipe 8 to perform necessary and sufficient turbidity management, there is no need to provide a turbidity meter in the drain pipe from each filtration pond.

【0018】なお、ろ過池の形式は任意であり、流入弁
等は、いわゆる弁に限らず、サイホンや空封トラップ等
の他の流入流出装置を適宜用いることができ、ろ過池の
設置数も上記形態例に限定されるものではない。
The type of the filtration basin is arbitrary, and the inflow valve and the like are not limited to so-called valves, and other inflow and outflow devices such as siphons and empty traps can be used as appropriate. It is not limited to the above embodiment.

【0019】[0019]

【発明の効果】以上説明したように、本発明によれば、
浄水場での水回収率の向上が図れるとともに、濁度を所
定値以下、例えば0.1度以下に確実に維持することが
できる。
As described above, according to the present invention,
The water recovery rate at the water purification plant can be improved, and the turbidity can be reliably maintained at a predetermined value or less, for example, 0.1 degrees or less.

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

【図1】 本発明のろ過池の一形態例を示す系統図であ
る。
FIG. 1 is a system diagram showing one embodiment of a filtration pond of the present invention.

【符号の説明】[Explanation of symbols]

A,B,C,D…ろ過池、1…原水渠、2a,2b,2
c,2d…流入弁、3a,3b,3c,3d…流出弁、
4…浄水池、5a,5b,5c,5d…排水弁、6a,
6b,6c,6d…捨水弁、7a,7b,7c,7d…
捨水管、8…集合捨水管、9…捨水ポンプ、10…捨水
流量計、11…濁度計、12a,12b,12c,12
d…ろ過流量計、13…サンプリング管、14…サンプ
リング弁、15…捨水排出管、16,17…切換弁、1
8…エアギャップ
A, B, C, D ... filtration pond, 1 ... raw culvert, 2a, 2b, 2
c, 2d ... inflow valves, 3a, 3b, 3c, 3d ... outflow valves,
4 ... water purifier, 5a, 5b, 5c, 5d ... drain valve, 6a,
6b, 6c, 6d ... drain valve, 7a, 7b, 7c, 7d ...
Drainage pipes, 8: Drainage pipes, 9: Drainage pumps, 10: Drainage flow meters, 11: Turbidity meters, 12a, 12b, 12c, 12
d: Filtration flow meter, 13: sampling pipe, 14: sampling valve, 15: waste water discharge pipe, 16, 17, switching valve, 1
8. Air gap

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C02F 1/00 (72)発明者 田名部 直勝 東京都中央区京橋1丁目3番3号 前澤工 業株式会社内──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code FI C02F 1/00 (72) Inventor Naokatsu Tanabe 1-3-3 Kyobashi, Chuo-ku, Tokyo Inside Maezawa Kogyo Co., Ltd.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 原水渠と、該原水渠にそれぞれ流入弁を
介して接続した複数のろ過池と、該ろ過池にそれぞれ流
出弁を介して接続した浄水池と、各ろ過池からの逆洗排
水を排出するそれぞれの排水弁と、各ろ過池にそれぞれ
捨水弁を介して接続した捨水管と、各捨水管を合流して
捨水を前記原水渠に戻す集合捨水管と、該集合捨水管に
設けられた捨水ポンプ,流量計及び濁度計とを備えてい
ることを特徴とするろ過池。
1. A raw water culvert, a plurality of filtration ponds connected to the raw culvert via respective inflow valves, a water purification ponds connected to the filtration ponds via respective outflow valves, and backwashing from each of the filtration ponds. A drain valve connected to each of the drainage valves for discharging drain water, each filtration pond through a drain valve, a drain pipe connected to each drain pipe to return drain water to the raw water conduit, A filtration pond comprising a waste water pump, a flow meter and a turbidity meter provided in a water pipe.
【請求項2】 請求項1記載のろ過池の運転方法であっ
て、ろ過池の逆洗操作終了後、前記捨水弁を開いて捨水
ポンプを作動させ、前記濁度計で捨水の濁度を測定しな
がら捨水ポンプの流量を徐々に増加させ、捨水の濁度が
設定濁度以下となり、ろ過速度が設定速度になったとき
に捨水操作を終了し、前記流出弁を開いて捨水弁を閉
じ、通常のろ過運転に移行することを特徴とするろ過池
の運転方法。
2. The method for operating a filter pond according to claim 1, wherein after the backwash operation of the filter pond, the water drain valve is opened to operate a water drain pump, and the water is drained by the turbidity meter. While measuring the turbidity, gradually increase the flow rate of the drainage pump, the turbidity of the wastewater becomes equal to or less than the set turbidity, and when the filtration speed reaches the set speed, the drainage operation is completed, and the outflow valve is closed. A method for operating a filtration pond, comprising opening and closing a drain valve to shift to normal filtration operation.
【請求項3】 前記捨水操作の開始時に、捨水の濁度が
所定値を超えるときには、該捨水を集合捨水管から原水
渠に戻すことなく、原水渠入口前から分岐した捨水排出
管を介して捨水貯槽に排出することを特徴とする請求項
2記載のろ過池の運転方法。
3. When the turbidity of the waste water exceeds a predetermined value at the start of the waste water operation, the waste water discharged from the front of the raw sewer entrance is returned without returning the waste water from the collecting sewer pipe to the raw sewer. The method for operating a filtration pond according to claim 2, wherein the water is discharged to a wastewater storage tank via a pipe.
JP9202822A 1997-07-29 1997-07-29 Filtration pond and method for operation thereof Pending JPH1147511A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9202822A JPH1147511A (en) 1997-07-29 1997-07-29 Filtration pond and method for operation thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9202822A JPH1147511A (en) 1997-07-29 1997-07-29 Filtration pond and method for operation thereof

Publications (1)

Publication Number Publication Date
JPH1147511A true JPH1147511A (en) 1999-02-23

Family

ID=16463777

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9202822A Pending JPH1147511A (en) 1997-07-29 1997-07-29 Filtration pond and method for operation thereof

Country Status (1)

Country Link
JP (1) JPH1147511A (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
JP2002282612A (en) * 2001-03-28 2002-10-02 Fuji Electric Co Ltd Method for operating spontaneous equilibrium type quick filter basin
JP2003024938A (en) * 2001-07-10 2003-01-28 Japan Organo Co Ltd Membrane filter system and operation method therefor
JP2008142576A (en) * 2006-12-05 2008-06-26 Oji Nepia Kk Filtration apparatus and filtering method
JP2009285618A (en) * 2008-05-30 2009-12-10 Sanyo Electric Co Ltd Filtration system

Cited By (6)

* 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
JP2002282612A (en) * 2001-03-28 2002-10-02 Fuji Electric Co Ltd Method for operating spontaneous equilibrium type quick filter basin
JP2003024938A (en) * 2001-07-10 2003-01-28 Japan Organo Co Ltd Membrane filter system and operation method therefor
JP2008142576A (en) * 2006-12-05 2008-06-26 Oji Nepia Kk Filtration apparatus and filtering method
JP4699981B2 (en) * 2006-12-05 2011-06-15 王子ネピア株式会社 Filtration apparatus and filtration method
JP2009285618A (en) * 2008-05-30 2009-12-10 Sanyo Electric Co Ltd Filtration system

Similar Documents

Publication Publication Date Title
CN206081820U (en) Backflushing filtering device
KR100679231B1 (en) Flexible-fiber filter module
JP2004249168A (en) Operation method for water treatment device
JPWO2002081050A1 (en) Rainwater treatment apparatus and combined backwash method in combined sewer system
CN107010744A (en) A kind of micro- waste water water purifier
JPH1147511A (en) Filtration pond and method for operation thereof
KR101109014B1 (en) A Pipe Connector for Automatic Back Washing of Filter
CN203833728U (en) Double-water-outlet water purifier capable of prolonging service life of reverse osmosis (RO) film
KR102054310B1 (en) Automatic operation type rainwater reusing system
JP3417113B2 (en) Filter pond washing control device and control method using chromaticity meter
JPH11226311A (en) Self-washing type filtration apparatus and operation method thereof
CN204121982U (en) A kind of device alleviating or avoid external tubular ultra-filtration membrane and block
KR101978143B1 (en) The backwashing pilot method of non point pollutants reduction facility
KR102351729B1 (en) Rainwater filtration and storage device
JP2001205022A (en) Method for controlling filter basin equipment
RU2243022C1 (en) Filtration installation
CN209456179U (en) The water purifier that can be recycled
JP6005426B2 (en) Filtration system and method for cleaning filtration system
JPH026824A (en) Method and apparatus for filtration
JP2004290752A (en) Method for filtering confluent sewage at high speed
JP2002126415A (en) Natural balance type filtration device and method of cleaning filter media layer thereof
JP2002282612A (en) Method for operating spontaneous equilibrium type quick filter basin
CN105951942A (en) Movable sewer pipeline filter
KR200365421Y1 (en) A treatment plant of wastewater
JPS6068021A (en) Washing system for filter basin in filter plant

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20040603

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20070118

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20070123

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20070724