JPS6295107A - Method and device for cleaning filter basin - Google Patents

Method and device for cleaning filter basin

Info

Publication number
JPS6295107A
JPS6295107A JP60235593A JP23559385A JPS6295107A JP S6295107 A JPS6295107 A JP S6295107A JP 60235593 A JP60235593 A JP 60235593A JP 23559385 A JP23559385 A JP 23559385A JP S6295107 A JPS6295107 A JP S6295107A
Authority
JP
Japan
Prior art keywords
filter medium
cleaning
medium bed
duration
filter
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
JP60235593A
Other languages
Japanese (ja)
Inventor
Hisatomo Akazawa
尚友 赤澤
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 JP60235593A priority Critical patent/JPS6295107A/en
Publication of JPS6295107A publication Critical patent/JPS6295107A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To reduce the amt. of a fluid necessary for cleaning and the power consumption and to save the energy by applying several agitations for agitating the part in the vicinity of the surface of a filter medium bed before the filter medium bed is backwashed and the surface is cleaned. CONSTITUTION:The raw water is supplied from a raw water supply pipe 2 and filtered by the filter medium bed 3. The filtered water is discharged from a filtered water discharge pipe 5. The contaminants are collected by the filtered water discharge pipe 5. The contaminants are collected by the filter medium bed 3 and the pressure drop of the filter medium bed 3 is progressively increased. When the pressure drop exceeds a set pressure drop, whether the duration up to that time exceeds the set duration or not is judged. When the duration exceeds the set duration, the part in the vicinity of the surface of the filter medium bed 3 is agitated by a surface vicinity agitator 10, the clogging of the filter medium bed 3 is temporarily eliminated, and filtration is resumed. When the duration does not exceed the set duration, cleaning wherein backwashing and surface washing are simultaneously carried out, is applied, and filtration is continued.

Description

【発明の詳細な説明】 「産業上の利用分野」 本発明は、廃水を清澄濾過する濾過池においてその濾材
層を効果的に洗浄する洗浄方法及びその装置に関する。
DETAILED DESCRIPTION OF THE INVENTION "Field of Industrial Application" The present invention relates to a cleaning method and apparatus for effectively cleaning a filter layer in a filter pond for clarifying and filtering wastewater.

「従来の技術」 従来、廃水(以下原水という)を濾過する濾過池として
種々のものが知られているが、なかでも重力式粒状活性
炭濾過池は都市水道等の濾過池としてよ(採用されてい
る。第6図はこの活性炭濾過池1を示すもので、原水供
給管2から送り込まれた原水は、粒状活性炭層より成る
濾材層3を重力により自然流下し、その間に原水中の汚
濁物質が濾材層3に捕捉せしめられると同時に、これら
捕捉物質と濾材が形成する流路群を通過した原水が濾過
水として下部集水装置4から濾過氷取出管5を経て系外
に取り出されるようになっている。
``Prior art'' Various types of filters have been known for filtering wastewater (hereinafter referred to as raw water), but among them, gravity-type granular activated carbon filters have been used as filters for urban water supplies, etc. Figure 6 shows this activated carbon filtration pond 1. Raw water sent from a raw water supply pipe 2 flows down by gravity through a filter layer 3 consisting of a layer of granular activated carbon, and during this time, pollutants in the raw water are removed. At the same time as being captured by the filter medium layer 3, the raw water that has passed through the channel group formed by these captured substances and the filter medium is taken out of the system as filtered water from the lower water collection device 4 via the filtered ice removal pipe 5. ing.

また、濾過に伴って濾材層3中の汚濁物質が増大し、そ
の圧力損失が高まった場合釦は、逆流洗浄管(逆流洗浄
装り6を経て下部集水装置4から水を噴出させ、濾材層
3を浮動状態にして洗浄する。と同時に、表面流#f(
表面洗浄装置)7から圧力水を噴射し、濾材相互の衝突
摩擦を増大させて洗浄効果を高めるようになっている。
In addition, if the contaminants in the filter layer 3 increase due to filtration and the pressure loss increases, the button will cause water to be jetted out from the lower water collection device 4 through the backwash pipe (backwash device 6) and Layer 3 is washed in a floating state. At the same time, surface flow #f (
Pressure water is injected from the surface cleaning device (7) to increase the collision friction between the filter media and enhance the cleaning effect.

なお、図中8はトラフ、9は洗浄排水管、2 a、  
5 a、6a。
In addition, in the figure, 8 is a trough, 9 is a cleaning drain pipe, 2 a,
5a, 6a.

7a、9aは順に原水弁、濾過水弁、逆流洗浄弁、表面
洗浄弁、洗浄排水弁である。
7a and 9a are, in order, a raw water valve, a filtered water valve, a backwash valve, a surface washing valve, and a washing drain valve.

「発明が解決しようとする問題点」 しかしながら、上記濾過池1では、濾過水質を良好に維
持するには逆流洗浄及び表面洗浄をかなり頻繁に行わな
ければならず、その結果、洗浄に要する水量や動力が増
大し、運転費が嵩んでしまうという不具合があった。
"Problems to be Solved by the Invention" However, in the filtration basin 1, backwashing and surface washing must be performed quite frequently in order to maintain good filtration water quality, and as a result, the amount of water required for washing is reduced. The problem was that the power required increased and operating costs increased.

本発明は、上記事情に鑑みてなされたもので、逆流洗浄
及び表面洗浄の間隔を延ばすことにより省エネルギーを
図った濾過池の洗浄方法及びその装置を提供することを
目的とする。
The present invention was made in view of the above circumstances, and an object of the present invention is to provide a method and apparatus for cleaning a filtration basin that saves energy by extending the interval between backwashing and surface cleaning.

r問題点を解決するだめの手段」 上記目的を達成するために、本発明の方法は、濾材層を
逆流洗浄しかつ表面洗浄をする洗浄工程に移る前に、濾
材層の表面近傍部分を攪拌する表面近傍攪拌工程を適数
回実施するようにしたもので、また、本発明の装置は、
濾材層を逆流洗浄する逆流洗浄装置と、濾材層を表面洗
浄する表面洗浄装置と、濾材層の表面近傍部分を攪拌す
る表面近傍攪拌装置とから構成したものである。
In order to achieve the above object, the method of the present invention includes stirring the near surface portion of the filter layer before proceeding to the cleaning step of backwashing the filter layer and cleaning the surface. The device of the present invention is designed to carry out the near-surface stirring step an appropriate number of times.
It is composed of a backwashing device for backwashing the filtering medium layer, a surface cleaning device for surface washing the filtering medium layer, and a near-surface agitation device for stirring the portion near the surface of the filtering medium layer.

「作 用」 本発明においては、濾材層が閉塞した段階で従来同様こ
れを逆流洗浄すると同時に表面洗浄するが、その洗浄を
実施する前に表面近傍攪拌装置により濾材層の表面近傍
部分のみを攪拌し、濾材ノーの閉塞を一時的に解消させ
て上記逆流洗浄及び表面洗浄までの時間を延ばす。
"Function" In the present invention, when the filter layer becomes clogged, it is backwashed and the surface is washed at the same time as in the conventional method, but before the cleaning is carried out, only the portion near the surface of the filter layer is stirred by a near-surface stirring device. Then, the blockage of the filter medium is temporarily cleared and the time until the above-mentioned backwashing and surface cleaning is extended.

「実施例」 第1図ないし第6図は本発明の装置の一実癩例を示すも
ので、従来例と基本構造を同一にする部分については従
来例と同一の符号を付してその説明を省略する。
``Example'' Figures 1 to 6 show an example of the device of the present invention, and parts having the same basic structure as the conventional example are given the same reference numerals as the conventional example and will be explained. omitted.

図中lOは図示しない圧力水供給管に連絡された攪拌管
(表面近傍攪拌装置)である。この攪拌管10は、濾過
池1の外部に位置するその所定位置に攪拌弁11を備え
たもので、濾過池1の内部では濾材層3の内方部でその
表面からの深さhが10〜50cmになる高さに水平に
配設されており、また、その濾材層3の内方部に位置す
る埋設管部101Lにはその長手方向の適宜箇所に分岐
管10bが連設されている。そして、埋設管部10aと
各亦岐管10bの各終端部は閉塞されると共に、その各
管壁の上部側には、管の軸線を中心として管の左右に例
えば各45度の角度で振り分けられて上方に向く複数の
ノズル10cが管の長手方向に所定のピッチで設けられ
ている。
In the figure, lO is a stirring pipe (near surface stirring device) connected to a pressure water supply pipe (not shown). This stirring tube 10 is equipped with a stirring valve 11 at a predetermined position located outside the filter basin 1, and inside the filter basin 1, the depth h from the surface of the inner part of the filter medium layer 3 is 10. It is arranged horizontally at a height of ~50 cm, and branch pipes 10b are connected to the buried pipe section 101L located in the inner part of the filter medium layer 3 at appropriate locations in the longitudinal direction. . Then, the terminal ends of the buried pipe portion 10a and each branch pipe 10b are closed, and on the upper side of each pipe wall, the pipes are distributed at an angle of, for example, 45 degrees to the left and right of the pipe with the axis of the pipe as the center. A plurality of nozzles 10c facing upward are provided at a predetermined pitch in the longitudinal direction of the tube.

しかして、上記装置では濾材層3の逆流洗浄及び表面洗
浄は、従来同様、逆流洗浄管6及び表面洗浄管7により
実施する一方、攪拌管1oにより濾材層3の表面近傍部
分を攪拌する。すなわち、攪拌弁11を開放して攪拌管
10のノズル10cから圧力水を噴出する。すると、圧
力水は濾材層3の内方部から上方に向けて噴出し、濾材
層3の表面近傍部分を攪拌し、濾材相互を衝突摩擦させ
て汚濁物質を分散させながらこれを圧送除去すも濾材層
3における閉塞は濾材層30表面近傍部分に生じやすい
から、その部分のみを攪拌洗浄するだげでも濾材層3の
閉塞を効果的に解消することができ、しかも、この表面
近傍攪拌に要する水量及び消費動力は逆流洗浄及び表面
洗浄の場合に比し極めて少ない。
Thus, in the above apparatus, backwashing and surface cleaning of the filter layer 3 are carried out by the backwash tube 6 and the surface cleaning tube 7, as in the conventional method, while the portion near the surface of the filter layer 3 is stirred by the stirring tube 1o. That is, the stirring valve 11 is opened and pressurized water is spouted from the nozzle 10c of the stirring tube 10. Then, the pressurized water is ejected upward from the inside of the filter layer 3, agitates the area near the surface of the filter layer 3, causes the filter media to collide and rub against each other, dispersing the pollutants and removing them under pressure. Since blockage in the filter medium layer 3 is likely to occur in the vicinity of the surface of the filter medium layer 30, the blockage in the filter medium layer 3 can be effectively eliminated by stirring and cleaning only that area. The amount of water and power consumption is much lower than in backwashing and surface cleaning.

次に、本発明の方法の一実施例を第4図に基づいて説明
する。
Next, an embodiment of the method of the present invention will be described based on FIG.

先ず、通常通り原水供給管2がら原水を供給して濾材層
3により濾過し、Ilカ過水取出管5より濾過水を連続
的に取出す。すると、濾材層3に原水中の汚濁物質が捕
捉され、これが増大して瀞材層3における圧力損失Pが
徐々に増大していく。この圧力損失Pが設定圧カ損失P
s未滴の場合はそのまま濾過を継続するが、圧力損失P
が設定圧カ損失PB以上になった時には、それまでの所
要時間tが設定所要時間t8 を超えたか否かを判定す
る。そして、所要時間tが設定所要時間t を超えてい
れば表面近傍攪拌装[10により濾材層3の表面近傍部
分を攪拌し、これにより濾材層3の閉塞を一時的に解消
して再び濾過を開始する。また、上記所要時間tが設定
所要時間t を超えていない場合は逆流洗浄と表面洗浄
を同時に行う洗浄工程に移り、濾材層3の閉塞を完全に
解消し、濾過を継続する。
First, raw water is supplied through the raw water supply pipe 2 and filtered through the filter medium layer 3 as usual, and filtered water is continuously taken out from the Il filter water take-out pipe 5. Then, the pollutants in the raw water are captured by the filter layer 3, and this increases, and the pressure loss P in the filter layer 3 gradually increases. This pressure loss P is the set pressure loss P
If there are no drops, continue filtration, but the pressure loss P
When the pressure loss becomes equal to or greater than the set pressure loss PB, it is determined whether the required time t up to that point exceeds the set required time t8. If the required time t exceeds the set required time t, the near-surface portion of the filter layer 3 is stirred by the near-surface stirring device [10, thereby temporarily eliminating the blockage of the filter layer 3 and starting the filtration again. Start. Further, if the required time t does not exceed the set required time t 2 , the process moves to a cleaning step in which backwashing and surface cleaning are performed simultaneously, the blockage of the filter medium layer 3 is completely eliminated, and filtration is continued.

すなわち、上記方法では、圧力損失Pが設定圧力損失P
8を超えたとしても、それが設定所要時間t  より遅
い段階で超えたものならば、濾材層3の閉塞の程度はま
だ軽微であると判断して表面近傍攪拌工程に移ってその
閉塞を一時的に解消して濾過を継続し、また、圧力損失
Pが設定所要時間を以内に設定圧力損失P8を超えてし
まった場合は、濾材層3の閉塞の程度はかなり進行して
いると判断して本格的な逆流洗浄・表面洗浄による洗浄
工程に移る。
That is, in the above method, the pressure loss P is equal to the set pressure loss P
Even if it exceeds 8, if it is exceeded at a stage later than the set required time t, it is judged that the degree of blockage of the filter medium layer 3 is still minor, and the blockage is temporarily removed by moving to the near-surface stirring process. If the problem is resolved and filtration continues, and if the pressure loss P exceeds the set pressure loss P8 within the set required time, it is determined that the degree of blockage in the filter medium layer 3 has progressed considerably. Then move on to the cleaning process using full-scale backwashing and surface cleaning.

ここで、濾材層3における閉塞は通常濾材層3の表面近
傍部分から生じるから、閉塞の程度の低い段階で表面近
傍の攪拌を行うと極めて有効である。このため、上記の
ように本格的な洗浄工程に移る前に表面近傍攪拌を実施
するようにすると、本格的な洗浄工程の回数のかなりの
部分をこの表面近傍攪拌に置き換えることが実際に可能
である。
Here, since blockage in the filter medium layer 3 usually occurs from a portion near the surface of the filter medium layer 3, it is extremely effective to perform stirring near the surface at a stage when the degree of blockage is low. Therefore, if near-surface agitation is performed before moving on to the full-scale cleaning process as described above, it is actually possible to replace a significant portion of the number of full-scale cleaning processes with this near-surface agitation. be.

したがって、洗浄に要する水量や動力消費の多い上記洗
浄工程の回数が減じられ、その代りに水量や動力消費の
極めて少ない表面近傍攪拌工程が7111わることにな
るから、全体の消費水量や動力は従来に比し大幅に低減
される。
Therefore, the number of times of the above-mentioned cleaning process, which consumes a large amount of water and power, is reduced, and in its place, the stirring process near the surface, which consumes very little water and power, is performed, so the overall amount of water and power consumed are reduced compared to those of the previous one. This is significantly reduced compared to .

また、第5図は本発明の方法の他の実施例を示すもので
、この例においては、圧力損失Pが設定圧力損失Pa1
以上になったときに表面近傍攪拌工程に入るが、この表
面近傍攪拌工程の回数Nが設定回数Nsになるまでこれ
を繰り返す。そして、設定回数N8になった時にはじめ
て逆流洗浄・表面洗浄から成る洗浄工程に移る。この方
法によっても、上記の場合と同様、本格的な洗浄工程の
回数を減らすことができ、省エネルギーを図ることがで
きる。
Further, FIG. 5 shows another embodiment of the method of the present invention, in which the pressure loss P is the set pressure loss Pa1
When the above is reached, the near-surface stirring step is started, and this is repeated until the number of times N of this near-surface stirring step reaches the set number Ns. Then, only when the set number of times N8 has been reached does the cleaning process consisting of backflow cleaning and surface cleaning proceed. With this method, as in the case described above, the number of full-scale cleaning steps can be reduced and energy can be saved.

ところで、上記においては、攪拌管10に複数のノズル
10cを設けたが、その位置は図示の位置に限るもので
はないし、ノズル10cの代りにノズル孔を形成してい
ってもよい。また、攪拌管10を通じて圧力水を噴出さ
せるのではな(て、圧縮空気を噴出させるようにしても
よく、これは逆流洗浄及び表面洗浄についても同様であ
る。さらに、上記実施例では濾材として粒状活性炭を用
いた濾過池lについて説明したが、濾材の種類は砂等他
のものでもよいことは熱論である。
Incidentally, in the above description, the stirring tube 10 is provided with a plurality of nozzles 10c, but their positions are not limited to the illustrated positions, and nozzle holes may be formed in place of the nozzles 10c. In addition, instead of jetting out pressurized water through the stirring tube 10, compressed air may be jetted out, and the same applies to backwashing and surface cleaning.Furthermore, in the above embodiment, granular Although we have described a filter using activated carbon, it is a matter of course that other types of filter media, such as sand, may also be used.

「発明の効果」 以上説明したように、本発明は、濾材層が閉塞した段階
でこれを逆流洗浄すると同時に表面洗浄するが、その洗
浄を実施する前に濾材層の閉塞の程度が軽微な段階で濾
材層の表面近傍部分のみを攪拌し、これにより濾材層の
閉塞を一時的に解消して上記逆流洗浄及び表面洗浄まで
の時間を延ばすようにしたから、洗浄に要する流体量や
消費動力が減少して省エネルギーを図ることができると
いう効果を奏する。
"Effects of the Invention" As explained above, the present invention performs backflow cleaning and surface cleaning at the stage when the filter media layer is clogged. By stirring only the area near the surface of the filter layer, this temporarily relieves the blockage of the filter layer and extends the time required for backwashing and surface cleaning, reducing the amount of fluid and power consumption required for cleaning. This has the effect of reducing energy consumption and saving energy.

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

第1図ないし第3図は本発明の装置の一実施例を示すも
ので、第1図は全体概略図、第2図は要部断面略図、第
3図は第2図のff−1矢視断面図、また、第4図は本
発明の方法の一実施例を示すフローチャート図、第5図
は同じく他の実施例を示すフローチャート図、第6図は
従来例を示す全体概略図である。 3・・・・・・濾材層、6・・・・・・逆流洗浄管(逆
流洗浄装面、7・・・・・・表面洗浄管(表面洗浄装置
)、10・・・・・・攪拌管(表面近傍攪拌装置)。
1 to 3 show an embodiment of the apparatus of the present invention, in which FIG. 1 is an overall schematic diagram, FIG. 2 is a schematic sectional view of the main part, and FIG. 3 is an arrow ff-1 in FIG. 2. 4 is a flowchart showing one embodiment of the method of the present invention, FIG. 5 is a flowchart showing another embodiment, and FIG. 6 is an overall schematic diagram showing a conventional example. . 3... Filter media layer, 6... Backflow cleaning tube (backflow cleaning device surface, 7... Surface cleaning tube (surface cleaning device), 10... Stirring tube (near surface stirring device).

Claims (2)

【特許請求の範囲】[Claims] (1)濾材層を逆流洗浄しかつ表面洗浄をする洗浄工程
に移る前に、濾材層の表面近傍部分を攪拌する表面近傍
攪拌工程を適数回実施することを特徴とする濾過池の洗
浄方法。
(1) A method for cleaning a filtration basin, characterized by carrying out a near-surface agitation step for stirring the near-surface portion of the filter layer an appropriate number of times before proceeding to a cleaning step for backwashing the filter layer and surface cleaning. .
(2)濾材層を逆流洗浄する逆流洗浄装置と、濾材層を
表面洗浄する表面洗浄装置と、濾材層の表面近傍部分を
攪拌する表面近傍攪拌装置とから成ることを特徴とする
濾過池の洗浄装置。
(2) Cleaning of a filter basin characterized by comprising a backwashing device for backwashing the filtering medium layer, a surface cleaning device for surface washing the filtering medium layer, and a near-surface agitation device for stirring the portion near the surface of the filtering medium layer. Device.
JP60235593A 1985-10-22 1985-10-22 Method and device for cleaning filter basin Pending JPS6295107A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60235593A JPS6295107A (en) 1985-10-22 1985-10-22 Method and device for cleaning filter basin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60235593A JPS6295107A (en) 1985-10-22 1985-10-22 Method and device for cleaning filter basin

Publications (1)

Publication Number Publication Date
JPS6295107A true JPS6295107A (en) 1987-05-01

Family

ID=16988298

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60235593A Pending JPS6295107A (en) 1985-10-22 1985-10-22 Method and device for cleaning filter basin

Country Status (1)

Country Link
JP (1) JPS6295107A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0615110A (en) * 1991-12-26 1994-01-25 Ishikawa Pref Gov Cleaning device for filter basin

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5355571A (en) * 1976-10-29 1978-05-20 Hitachi Metals Ltd Surface washer for filtering sand
JPS58124507A (en) * 1982-01-18 1983-07-25 Fuso Kensetsu Kogyo Kk Method for washing surface of pressure type multi layer filter basin

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5355571A (en) * 1976-10-29 1978-05-20 Hitachi Metals Ltd Surface washer for filtering sand
JPS58124507A (en) * 1982-01-18 1983-07-25 Fuso Kensetsu Kogyo Kk Method for washing surface of pressure type multi layer filter basin

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0615110A (en) * 1991-12-26 1994-01-25 Ishikawa Pref Gov Cleaning device for filter basin

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