JP2573454Y2 - Activated carbon water treatment tank - Google Patents

Activated carbon water treatment tank

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Publication number
JP2573454Y2
JP2573454Y2 JP1992049127U JP4912792U JP2573454Y2 JP 2573454 Y2 JP2573454 Y2 JP 2573454Y2 JP 1992049127 U JP1992049127 U JP 1992049127U JP 4912792 U JP4912792 U JP 4912792U JP 2573454 Y2 JP2573454 Y2 JP 2573454Y2
Authority
JP
Japan
Prior art keywords
water
chamber
activated carbon
treated
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.)
Expired - Fee Related
Application number
JP1992049127U
Other languages
Japanese (ja)
Other versions
JPH063484U (en
Inventor
英幸 臼井
教由 小阪
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.)
Tokyu Car Corp
Original Assignee
Tokyu Car Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tokyu Car Corp filed Critical Tokyu Car Corp
Priority to JP1992049127U priority Critical patent/JP2573454Y2/en
Publication of JPH063484U publication Critical patent/JPH063484U/en
Application granted granted Critical
Publication of JP2573454Y2 publication Critical patent/JP2573454Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】本考案は、主として下水三次処
理、プール水の清浄化、ゴルフ場の周辺池の浄化等にオ
ゾン処理と併用して用いられ、水中に溶解している有機
物を吸着除去するとともに水中に残留するオゾンを分解
削減する活性炭水処理槽に関する。
This invention is mainly used in combination with ozone treatment for the tertiary treatment of sewage, the purification of pool water, the purification of ponds around golf courses, etc., and the adsorption and removal of organic substances dissolved in water. And an activated carbon water treatment tank for decomposing and reducing ozone remaining in water.

【0002】[0002]

【従来の技術】従来、水中に溶解している有機物を除去
する方法として活性炭が利用されている。
2. Description of the Related Art Conventionally, activated carbon has been used as a method for removing organic substances dissolved in water.

【0003】該活性炭を利用する方法としては、主に、
円筒タンク状の槽内に粒状活性炭を充填し、槽の上方か
ら有機物の溶解している被処理水を供給し、この被処理
水が粒状活性炭層を通過して槽の下方に至る間に有機物
を吸着除去する方法、及び前記方法とは逆に、槽の下方
から有機物が溶解している被処理水を供給して、該供給
された被処理水とともに槽内の粒状活性炭を流動させな
がら有機物を吸着除去するという方法等が行われてい
る。
[0003] As a method of utilizing the activated carbon, mainly,
A cylindrical tank is filled with granular activated carbon, and water to be treated in which organic substances are dissolved is supplied from above the tank.The water is passed through the granular activated carbon layer to reach the lower part of the tank. A method for adsorbing and removing the organic matter, and conversely to the above-mentioned method, supplying treated water in which the organic matter is dissolved from below the tank, and flowing the granular activated carbon in the tank together with the supplied treated water to remove the organic matter. And the like have been carried out.

【0004】[0004]

【考案が解決しようとする課題】前記前者の方法では、
槽内に充填した粒状活性炭の層が固定されているため、
長時間にわたって使用した場合には、被処理水中に含ま
れるゴミ等によって目詰まりを起こして流れが悪くな
り、効率のよい吸着除去を行うためには比較的頻繁に逆
洗浄を行って前記粒状活性炭層の目詰まりを除去しなけ
ればならなかった。
[Problem to be solved by the invention] In the former method,
Because the layer of granular activated carbon filled in the tank is fixed,
When used for a long period of time, dust and the like contained in the water to be treated cause clogging, which deteriorates the flow. In order to perform efficient adsorption and removal, backwashing is performed relatively frequently to remove the granular activated carbon. The clogging of the layers had to be removed.

【0005】さらに、槽内に充填する粒状活性炭の層が
厚くなるため、上方から供給される有機物の溶解してい
る被処理水が、粒状活性炭層を通過する際には圧力損失
が大きくなり、被処理水を供給するポンプとして動力の
大きなものが必要であった。
[0005] Further, since the layer of granular activated carbon filled in the tank becomes thick, the water to be treated, which is supplied with an organic substance and dissolved therein, passes through the granular activated carbon layer, resulting in a large pressure loss. A pump with a large power was required to supply the water to be treated.

【0006】また、前記後者の方法によれば、粒状活性
炭は供給された被処理水とともに流動させられるため、
目詰まりを起こすことがなく逆洗浄の必要はなくなる
が、前者の方法のごとく固定された粒状活性炭層を利用
した場合と同等の処理効果をあげるためには、大量の粒
状活性炭が必要となり処理槽が大型化するという問題が
あった。
According to the latter method, since the granular activated carbon is caused to flow together with the supplied water to be treated,
Backwashing is not required without clogging, but a large amount of granular activated carbon is required to achieve the same treatment effect as when using a fixed granular activated carbon layer as in the former method. However, there was a problem that the size became large.

【0007】さらに、長時間にわたって使用した場合に
は、供給された被処理水とともに粒状活性炭が流動させ
られるため、該粒状活性炭の一部が砕ける等して細かく
なり、処理水と一緒に流失してしまう等のことがあっ
た。
Further, when the granular activated carbon is used for a long time, the granular activated carbon is caused to flow together with the supplied water to be treated, so that part of the granular activated carbon becomes fine due to crushing or the like, and the granular activated carbon flows away together with the treated water. And so on.

【0008】本考案は前記事情に鑑みてなされたもの
で、有機物の溶解した被処理水が粒状活性炭層を通過す
る際の圧力損失を少なくするとともに、粒状活性炭層の
逆洗浄を不要として、さらにその流失を防止でき、さら
には設置のための場所をとらずコンパクトな活性炭処理
水槽を提供することを目的とする。
The present invention has been made in view of the above circumstances, and reduces the pressure loss when water to be treated in which organic substances are dissolved passes through a granular activated carbon layer, and eliminates the need for backwashing of the granular activated carbon layer. An object of the present invention is to provide a compact activated carbon treatment water tank which can prevent the spillage and can save space for installation.

【0009】[0009]

【課題を解決するための手段】前記課題を解決するた
め、本考案は、上下面が閉じられた密閉箱形状で、内部
がそれぞれ縦に配置した多孔材によって導水室、濾過
室、空室、活性炭室及び排水室に仕切られ、さらに前記
導水室及び濾過室が、それぞれの略中央部に設けた隔壁
によって二分割され、該二分割された導水室の二つの部
屋にはそれぞれ導水口が設けられ、上面にはそれぞれ逆
洗水排出口が設けられ、前記分割された濾過室の二つの
部屋内には下部にそれぞれ散気管が設けられるとともに
それぞれ濾材が充填され、さらに前記活性炭室には粒状
活性炭が充填され、前記排水室には処理水排出口が設け
られてなる構成としたものである。
In order to solve the above-mentioned problems, the present invention is directed to a water-guiding chamber, a filtration chamber, an empty chamber, and the like, which are formed in a closed box shape having upper and lower surfaces closed, and each of which has a vertically arranged porous material. Partitioned into an activated carbon chamber and a drainage chamber, the water conduction chamber and the filtration chamber are further divided into two by a partition wall provided at substantially the center of each of the two chambers. Backwash water discharge ports are provided on the upper surface, respectively.Aperture pipes are respectively provided at the lower portions in the two chambers of the divided filtration chamber, and a filter medium is filled therein, and the activated carbon chamber is granular. Activated carbon is filled, and the drainage chamber is provided with a treated water discharge port.

【0010】[0010]

【作用】本考案において、被処理水としてオゾン接触溶
解させた水を使用すれば、粒状濾材24、細石等25、
27及び粒状活性炭26への微生物の付着及び繁殖を防
止できるとともに、前記オゾンが粒状活性炭に吸着され
た有機物を酸化分解し寿命をさらに延長できる。
According to the present invention, if water to be dissolved in contact with ozone is used as the water to be treated, the particulate filter medium 24, fine stones and the like 25,
The adhesion and propagation of microorganisms to the granular activated carbon 27 and the granular activated carbon 26 can be prevented, and the ozone can oxidize and decompose the organic matter adsorbed on the granular activated carbon to further extend the life.

【0011】本考案では、有機物の溶解した被処理水
が、導水室の二分割された部屋2及び3に設けられた導
水口11及び12から内部に取り入れられ、その流速が
減速される。
In the present invention, the water to be treated, in which the organic matter is dissolved, is taken into the inside from the water supply ports 11 and 12 provided in the two divided chambers 2 and 3 of the water supply chamber, and the flow velocity thereof is reduced.

【0012】つぎに、前記被処理水は、濾過室の二分割
された部屋4及び5内に充填された粒状濾材24を通過
することによって濾過されるとともに水の流れが平準化
される。
Next, the water to be treated is filtered by passing through the particulate filter medium 24 filled in the two divided chambers 4 and 5 of the filtration chamber, and the flow of water is leveled.

【0013】さらに、前記被処理水は空室6を通り、濾
過室7の細石等25間を通過し、粒状活性炭26が充填
された活性炭室8に流入する。
Further, the water to be treated passes through the empty chamber 6, passes between the fine stones 25 and the like in the filtration chamber 7, and flows into the activated carbon chamber 8 filled with granular activated carbon 26.

【0014】そして、この活性炭室8を通過する際に被
処理水中に溶解している有機物が吸着除去されるととも
に、残留している溶存オゾンが低減される。
When passing through the activated carbon chamber 8, the organic matter dissolved in the water to be treated is adsorbed and removed, and the remaining dissolved ozone is reduced.

【0015】その後、前記活性炭室8を通過した処理水
は、濾過室9の細石等27間を通り、排水室10に至
り、そこに設けられた排出口15から外部の再利用先に
排出される。
Thereafter, the treated water that has passed through the activated carbon chamber 8 passes between the fine stones 27 in the filtration chamber 9, reaches the drain chamber 10, and is discharged from a discharge port 15 provided therein to an external reuse destination. You.

【0016】なお、前記本考案の処理槽Aを長時間にわ
たって使用すると、前記粒状濾材24が被処理水中に含
まれるゴミ等により目詰まりを起こす。
If the treatment tank A of the present invention is used for a long time, the particulate filter medium 24 is clogged by dust and the like contained in the water to be treated.

【0017】本考案では、該目詰まりが圧力センサー2
1によって検出される。
In the present invention, the clogging is caused by the pressure sensor 2
1 is detected.

【0018】すなわち、導水パイプ44、28及び29
内の水圧が前記目詰まりにより一定値以上に達すると、
まず、導水自動操作バルブ16が閉じ、逆洗水排出自動
操作バルブ18が開放される。続いて、処理水出口自動
操作バルブ20が閉じられるとともに、電磁弁33が開
かれてエアー供給管35から散気管22にエアーが供給
される。
That is, the water guide pipes 44, 28 and 29
When the water pressure inside reaches a certain value or more due to the clogging,
First, the automatic water guide valve 16 is closed, and the automatic backwash water discharge valve 18 is opened. Subsequently, the process water outlet automatic operation valve 20 is closed, and the electromagnetic valve 33 is opened to supply air from the air supply pipe 35 to the air diffuser 22.

【0019】その結果、導水口12からの被処理水が導
水室1の一方の部屋3から濾過室51の一方の部屋5へ
供給され、さらに空室6に供給される。
As a result, the water to be treated from the water introduction port 12 is supplied from one room 3 of the water introduction room 1 to one room 5 of the filtration room 51 and further supplied to the empty room 6.

【0020】しかしながら、処理水出口自動操作バルブ
20が閉じられているため濾過室51の他方の部屋4へ
背面から流入してその内部の粒状濾材24を逆洗浄し、
該粒状濾材24間を浮上する気泡の働きも加わってゴミ
等を含んだ洗浄水が導水室1の一方の部屋2に押し戻さ
れ、逆洗水排出口13から逆洗水排出パイプ30を通っ
て外部に排出される。
However, since the treated water outlet automatic operation valve 20 is closed, it flows into the other chamber 4 of the filtration chamber 51 from the back and backwashes the particulate filter medium 24 therein.
The washing water containing dust and the like is pushed back to one room 2 of the water guide chamber 1 by the action of the air bubbles floating between the particulate filter media 24, and is passed through the backwash water discharge port 13 through the backwash water discharge pipe 30. It is discharged outside.

【0021】そして、一定時間、濾過室51の他方の部
屋4内の粒状濾材24の逆洗浄を行った後に電磁弁33
が閉じられ、散気管22へのエアーの供給が停止され、
さらに導水自動操作バルブ17及び逆洗水排出自動操作
バルブ18が閉じられる。
After the particulate filter medium 24 in the other chamber 4 of the filtration chamber 51 is backwashed for a certain period of time, the solenoid valve 33
Is closed, the supply of air to the air diffuser 22 is stopped,
Further, the automatic water guiding valve 17 and the automatic backwash water discharging valve 18 are closed.

【0022】つぎに濾過室51の一方の部屋5内の粒状
濾材24の逆洗浄が行われる。
Next, backwashing of the particulate filter medium 24 in one of the filtration chambers 51 is performed.

【0023】すなわち、逆洗水排出自動操作バルブ19
が開放させられるとともに導水自動操作バルブ16が開
放させられて、導水口11からの被処理水が導水室1の
他方の部屋2から濾過室51の他方の部屋4へ供給さ
れ、空室6を通って濾過室51の一方の部屋5の背面か
ら流入し、同時に電磁弁34が開かれてエアー供給管3
6から散気管23にエアーが供給され、濾過室51の一
方の部屋5内の粒状濾材24が前記と同様の方法で逆洗
浄され、ゴミ等を含んだ洗浄水が逆洗水排出口14から
逆洗水排出パイプ31を通って外部に排出される。
That is, the backwash water discharge automatic operation valve 19
Is opened and the automatic water guiding valve 16 is opened, and the water to be treated from the water introducing port 11 is supplied from the other room 2 of the water introducing chamber 1 to the other room 4 of the filtration chamber 51, and the empty room 6 is opened. Then, it flows in from the back of one of the chambers 5 of the filtration chamber 51, and at the same time, the solenoid valve 34 is opened to open the air supply pipe 3.
Air is supplied to the air diffuser 23 from 6, and the particulate filter medium 24 in one of the chambers 5 of the filtration chamber 51 is backwashed in the same manner as described above, and washing water containing dust and the like is discharged from the backwash water outlet 14. The water is discharged outside through the backwash water discharge pipe 31.

【0024】そして、一定時間の逆洗浄後に電磁弁34
が閉じられ、散気管23へのエアーの供給が停止され、
さらに逆洗水排出自動操作バルブ19が閉じられるとと
もに処理水出口自動操作バルブ20及び導水自動操作バ
ルブ17が開放させられる。
After the backwashing for a predetermined time, the solenoid valve 34
Is closed, the supply of air to the air diffuser 23 is stopped,
Further, the backwash water discharge automatic operation valve 19 is closed, and the treated water outlet automatic operation valve 20 and the water introduction automatic operation valve 17 are opened.

【0025】その結果、当初の状態となり、再び被処理
水の浄化が行われる。
As a result, the state becomes the initial state, and the water to be treated is purified again.

【0026】[0026]

【実施例】以下、本考案の一実施例を図面に基づいて説
明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described below with reference to the drawings.

【0027】図1は本考案の活性炭水処理槽Aの一部切
欠斜視図、図2は本考案の活性炭水処理槽Aを下水三次
処理系統に使用した場合を示す概念図である。
FIG. 1 is a partially cutaway perspective view of an activated carbon water treatment tank A of the present invention, and FIG. 2 is a conceptual diagram showing a case where the activated carbon water treatment tank A of the present invention is used in a sewage tertiary treatment system.

【0028】本考案の活性炭水処理槽Aは、例えば、図
2に示されているように下水処理工程における最終沈殿
池41、送水ポンプ42及びオゾン接触溶解槽43から
なる下水三次処理系統の一部を構成すること等により実
用化される。
The activated carbon water treatment tank A of the present invention is, for example, as shown in FIG. 2, a sewage tertiary treatment system including a final sedimentation tank 41, a water pump 42 and an ozone contact dissolution tank 43 in the sewage treatment step. It is put to practical use by constituting a part.

【0029】すなわち、本考案の活性炭水処理槽Aは、
図示されているように水浄化系統のオゾン接触溶解槽4
3の先に設けられ、オゾン接触溶解槽43によりオゾン
が溶解させられた被処理水を内部に取り込んで濾過及び
容存有機物の吸着除去、溶存オゾンの接触分解を行うも
のである。
That is, the activated carbon water treatment tank A of the present invention comprises:
As shown, the ozone contact dissolution tank 4 of the water purification system
The ozone-dissolving tank 43 is provided at the end of the tank 3, and the water to be treated in which ozone is dissolved by the ozone contact dissolving tank 43 is taken into the inside to perform filtration, adsorption and removal of dissolved organic matter, and catalytic decomposition of dissolved ozone.

【0030】本考案の活性炭水処理槽Aは、図1に示さ
れているように、上下面が閉じられた密閉箱形状に耐オ
ゾン性プラスチック等により構成され、その内部がそれ
ぞれ縦に配置した多孔材37で導水室1、濾過室51、
空室6、活性炭室8及び排水室10に仕切られて、オゾ
ンが溶解した被処理水を取り込んで濾過及び溶存有機物
の吸着除去、溶存オゾンの接触分解を行えるように構成
されている。
As shown in FIG. 1, the activated carbon water treatment tank A of the present invention is made of an ozone-resistant plastic or the like in a closed box shape having upper and lower surfaces closed, and the insides thereof are vertically arranged. The water introduction chamber 1, the filtration chamber 51,
The chamber is partitioned into an empty space 6, an activated carbon room 8, and a drainage room 10, and is configured to take in the water to be treated in which ozone is dissolved, and perform filtration, adsorption and removal of dissolved organic matter, and catalytic decomposition of dissolved ozone.

【0031】もっとも、図面実施例では、前記活性炭室
8の両側に細石等25、27を充填した濾過室7、9を
設け、前記活性炭室8内の粒状活性炭26を目詰まり等
から保護している。
In the embodiment shown in the drawings, filtration chambers 7 and 9 filled with fine stones 25 and 27 are provided on both sides of the activated carbon chamber 8 to protect the granular activated carbon 26 in the activated carbon chamber 8 from clogging and the like. I have.

【0032】さらに、前記導水室1の略中央部が隔壁3
8によって二つの部屋2及び3に二分割され、さらに、
図2に示されたオゾン接触溶解槽43でオゾン接触溶解
された被処理水を内部に導く導水口11及び12がそれ
ぞれ設けられ、該導水口11及び12には前記被処理水
の導水パイプ44を分岐した導水パイプ28及び29が
各々接続されている。
Further, a substantially central portion of the water guide chamber 1 is provided with a partition wall 3.
8 into two rooms 2 and 3;
Water inlets 11 and 12 for introducing the water to be treated, which has been ozone contact-dissolved in the ozone contact dissolving tank 43 shown in FIG. 2, are provided therein. Are connected to each other.

【0033】さらに、該導水パイプ28及び29には、
被処理水導入用の導水自動操作バルブ16及び17が各
々設けられ、前記導水パイプ44の適位置には圧力セン
サー21が取り付けられている。
Further, the water pipes 28 and 29 include:
Automatic water guiding valves 16 and 17 for introducing the water to be treated are provided, respectively, and a pressure sensor 21 is attached to an appropriate position of the water guiding pipe 44.

【0034】さらに、前記二つの部屋2及び3のそれぞ
れ上面には洗浄水排出用の逆洗水排出口13及び14が
設けられ、該逆洗水排出口13及び14にゴミ等を含ん
だ逆洗浄水を外部に排出するための逆洗水排出パイプ3
0及び31がそれぞれ接続されている。
Further, backwash water outlets 13 and 14 for washing water discharge are provided on the upper surfaces of the two chambers 2 and 3, respectively. Backwash water discharge pipe 3 for discharging wash water to the outside
0 and 31 are connected respectively.

【0035】さらに、該逆洗水排出パイプ30及び31
には、逆洗水排出自動操作バルブ18及び19が各々設
けられている。
Further, the backwash water discharge pipes 30 and 31
Are provided with backwash water discharge automatic operation valves 18 and 19, respectively.

【0036】濾過室51は、前記導水室1と同じくその
略中央部が隔壁38aによって二つの部屋4及び5に二
分割され、それぞれその内部に適当な濾材、例えば比重
の軽い粒状濾材24が充填されて構成され、さらに、そ
れぞれの部屋4及び5の下部には前記粒状濾材24の目
詰まりを洗浄するための散気管22及び23が設けら
れ、該散気管22及び23にはエアーを外部から供給す
るエアー供給管35及び36がそれぞれ接続されてい
る。
The filtration chamber 51 is divided into two chambers 4 and 5 by a partition 38a at a substantially central portion, similarly to the water guide chamber 1, and each of them is filled with an appropriate filter medium, for example, a granular filter medium 24 having a light specific gravity. Further, air diffusion tubes 22 and 23 for cleaning the clogging of the particulate filter medium 24 are provided below the respective rooms 4 and 5, and air is supplied to the air diffusion tubes 22 and 23 from the outside. Supply air supply pipes 35 and 36 are connected respectively.

【0037】さらに、該エアー供給管35及び36に
は、前記散気管22及び23へのエアー供給を制御する
電磁弁33及び34が各々設けられている。
Further, the air supply pipes 35 and 36 are provided with electromagnetic valves 33 and 34 for controlling air supply to the air diffusers 22 and 23, respectively.

【0038】つぎに、前記濾過室51の次に空室6が設
けられ、つぎに設けた活性炭室8の内部には粒状活性炭
26が充填され、該粒状活性炭26中を、オゾンが溶解
した被処理水が通過させられることによって被処理水中
に溶解している有機物が吸着除去され、残留している溶
存オゾンが低減されるように構成されている。
Next, an empty space 6 is provided next to the filtration chamber 51, and the inside of the activated carbon chamber 8 provided next is filled with granular activated carbon 26. The granular activated carbon 26 is filled with ozone dissolved therein. Organic matter dissolved in the water to be treated is adsorbed and removed by passing the treated water, so that the remaining dissolved ozone is reduced.

【0039】また、図面実施例では、活性炭室8の両側
に細石等25及び27を充填した濾過室7及び9が構成
されている。
In the embodiment shown in the drawings, filtration chambers 7 and 9 in which fine stones 25 and 27 are filled on both sides of the activated carbon chamber 8 are formed.

【0040】さらに、濾過室9に続いて排水室10が設
けられ、該排水室10には排出口15が設けられ、該排
出口15には処理済の水を外部の再利用先へ供給するた
めの処理水送水パイプ32が連結され、さらに、該処理
水送水パイプ32には処理水送水用の処理水出口自動操
作バルブ20が設けられる。
Further, a drainage chamber 10 is provided following the filtration chamber 9, and the drainage chamber 10 is provided with a discharge port 15, which supplies treated water to an external reuse destination. And a treated water outlet automatic operation valve 20 for supplying treated water is connected to the treated water supply pipe 32.

【0041】前記構成の本考案の活性炭処理水槽Aは、
図2に示されたオゾン接触溶解槽43でオゾン接触溶解
された被処理水が、導水パイプ44から導水パイプ28
及び29を通って導水室1の二つの部屋2及び3に設け
られた導水口11及び12から内部に取り入れられ、導
水室1において流速が減速される。
The activated carbon treatment water tank A according to the present invention having the above-described structure comprises:
The water to be treated, which has been ozone contact-dissolved in the ozone contact dissolution tank 43 shown in FIG.
And 29, the water is taken into the inside from the water introduction ports 11 and 12 provided in the two chambers 2 and 3 of the water introduction chamber 1, and the flow velocity is reduced in the water introduction chamber 1.

【0042】つぎに、前記被処理水は、濾過室の二つの
部屋4及び5内の粒状濾材24を通過することにより濾
過されるとともに水の流れが平準化される。
Next, the water to be treated is filtered by passing through the particulate filter medium 24 in the two chambers 4 and 5 of the filtration chamber, and the flow of water is leveled.

【0043】さらに、前記被処理水は空室6を通り、濾
過室7の細石等25間を通過し、活性炭室8の粒状活性
炭26間を通過する。
Further, the water to be treated passes through the empty room 6, passes between the fine stones 25 in the filtration room 7, and passes between the granular activated carbons 26 in the activated carbon room 8.

【0044】この粒状活性炭26間の通過において被処
理水中に溶解している有機物が吸着除去されるととも
に、残留している溶存オゾンが低減されることになる。
During the passage between the granular activated carbons 26, organic substances dissolved in the water to be treated are adsorbed and removed, and the remaining dissolved ozone is reduced.

【0045】その後、前記粒状活性炭26を通過した処
理水は、濾過室9の細石等27間を通って排水室10に
入り、そこに設けられた排出口15から処理水送水パイ
プ32を通って外部の再利用先へ排出供給される。
Thereafter, the treated water that has passed through the granular activated carbon 26 enters the drainage chamber 10 between the fine stones 27 of the filtration chamber 9 and the like, and passes through the treated water supply pipe 32 from the discharge port 15 provided therein. Emitted to external reuse destinations.

【0046】なお、前記処理槽1を長時間にわたって使
用すると、濾過室51の二つの部屋4及び5内に充填さ
れた粒状濾材24が被処理水中に含まれるゴミ等により
目詰まりを起こす。
When the treatment tank 1 is used for a long time, the particulate filter medium 24 filled in the two chambers 4 and 5 of the filtration chamber 51 is clogged by dust and the like contained in the water to be treated.

【0047】その結果、導水パイプ44、28及び29
内の圧力が上昇させられ、圧力センサー21によって上
昇圧力、すなわち目詰まりが検出される。
As a result, the water guide pipes 44, 28 and 29
The internal pressure is increased, and the pressure sensor 21 detects an increased pressure, that is, clogging.

【0048】前記圧力センサー21によって目詰まりが
検出されたら、導水自動操作バルブ16が閉じられ、逆
洗水排出自動操作バルブ18が開放される。
When the pressure sensor 21 detects clogging, the automatic water guiding valve 16 is closed and the automatic backwash water discharging valve 18 is opened.

【0049】続いて、処理水出口自動操作バルブ20が
閉じられるとともに、電磁弁33が開かれてエアー供給
管35から散気管22にエアーが供給され、濾過室51
の一方の部屋4側の粒状濾材24間を気泡が浮上し、粒
状濾材24間の目詰まりが解消される。
Subsequently, the treated water outlet automatic operation valve 20 is closed, the solenoid valve 33 is opened, and air is supplied from the air supply pipe 35 to the diffuser pipe 22, and the filtration chamber 51 is opened.
Bubbles float between the particulate filter media 24 on the one room 4 side, and clogging between the particulate filter media 24 is eliminated.

【0050】この状態において、被処理水は導水パイプ
44から導水パイプ29を通って導水室1の一方の部屋
3から濾過室51の一方の部屋5へ供給され、さらに空
室6に供給される。
In this state, the water to be treated is supplied from the water guide pipe 44 through the water guide pipe 29 to the one room 3 of the water guide chamber 1 to the one room 5 of the filtration chamber 51, and further to the empty room 6. .

【0051】しかしながら、処理水出口自動操作バルブ
20が閉じられているため、濾過室51の他方の部屋4
へ背面から流入してその内部の粒状濾材24を逆洗浄
し、前記気泡の働きも加わってゴミ等を含んだ洗浄水が
導水室1の一方の部屋2に押し出され、逆洗水排出口1
3から逆洗水排出パイプ30を通って外部に排出され
る。
However, since the treated water outlet automatic operation valve 20 is closed, the other chamber 4 of the filtration chamber 51 is closed.
Backwashing the particulate filter medium 24 therein, the washing water containing dust and the like is pushed out into one chamber 2 of the water introduction chamber 1 by the action of the air bubbles, and the backwash water outlet 1
3 is discharged outside through a backwash water discharge pipe 30.

【0052】そして、一定時間の逆洗浄後に電磁弁33
が閉じられ、散気管22へのエアーの供給が停止され、
さらに導水自動操作バルブ17及び逆洗水排出自動操作
バルブ18が閉じられる。
After the backwashing for a certain period of time, the solenoid valve 33
Is closed, the supply of air to the air diffuser 22 is stopped,
Further, the automatic water guiding valve 17 and the automatic backwash water discharging valve 18 are closed.

【0053】つぎに、濾過室51の一方の部屋5内の粒
状濾材24の逆洗浄が行われる。すなわち、逆洗水排出
自動操作バルブ19が開放させられるとともに導水自動
操作バルブ16が開放され、電磁弁34が開かれてエア
ー供給管36から散気管23にエアーが供給され、濾過
室51の一方の部屋5内の粒状濾材24が逆洗浄され、
ゴミ等を含んだ洗浄水が逆洗水排出口14から逆洗水排
出パイプ31を通って外部に排出される。
Next, the backwashing of the particulate filter medium 24 in one of the filtration chambers 51 is performed. That is, the backwash water discharge automatic operation valve 19 is opened, the water guide automatic operation valve 16 is opened, the solenoid valve 34 is opened, and air is supplied from the air supply pipe 36 to the air diffusion pipe 23. The granular filter medium 24 in the room 5 is back-washed,
Wash water containing dust and the like is discharged from the back wash water discharge port 14 to the outside through the back wash water discharge pipe 31.

【0054】そして、一定時間の洗浄後には電磁弁34
が閉じられ、散気管23へのエアーの供給が停止され、
さらに逆洗水排出自動操作バルブ19が閉じられるとと
もに、処理水出口自動操作バルブ20及び導水自動操作
バルブ17が開放させられる。
After the cleaning for a certain time, the solenoid valve 34
Is closed, the supply of air to the air diffuser 23 is stopped,
Further, the backwash water discharge automatic operation valve 19 is closed, and the treated water outlet automatic operation valve 20 and the water introduction automatic operation valve 17 are opened.

【0055】その結果、当初の状態となり、再び水の浄
化が行われる。
As a result, the state becomes the initial state, and the water is purified again.

【0056】[0056]

【考案の効果】本考案によれば、有機物の溶解した被処
理水を、粒状活性炭間に横方向から通過させるため圧力
損失を少なくできるとともに、粒状活性炭の逆洗浄が不
要となり、さらに活性炭の消耗が防止され、さらには濾
過部分と活性炭処理部分の一体化を図ることができ、設
置のための場所をとらずコンパクトに構成できる等の効
果が得られる。
According to the present invention, the water to be treated, in which organic matter is dissolved, is passed between the granular activated carbons in a lateral direction, so that the pressure loss can be reduced, and the backwashing of the granular activated carbon becomes unnecessary, and the activated carbon is further consumed. Is prevented, and the filtering portion and the activated carbon treatment portion can be integrated, and an effect such as a compact configuration without taking a place for installation can be obtained.

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

【図1】本考案の活性炭水処理槽の一部切欠斜視図であ
る。
FIG. 1 is a partially cutaway perspective view of an activated carbon water treatment tank of the present invention.

【図2】本考案の活性炭処水理槽を下水三次処理系統に
使用した場合を示す概念図である。
FIG. 2 is a conceptual diagram showing a case where the activated carbon treatment tank of the present invention is used in a sewage tertiary treatment system.

【符号の説明】[Explanation of symbols]

A 活性炭水処理槽 1 導水室 2、3 導水室の二つの部屋 4、5 濾過室の二つの部屋 6 空室 8 活性炭室 10 排水室 11、12 導水口 13、14 逆洗水排出口 15 排出口 22、23 散気管 24 粒状濾材 25、27 細石等 26 粒状活性炭 51 濾過室 A activated carbon water treatment tank 1 water introduction chamber 2, 3 two water introduction chambers 4, 5 two filtration rooms 6 vacant room 8 activated carbon room 10 drainage chamber 11, 12 water introduction port 13, 14 backwash water discharge port 15 drainage Outlets 22, 23 Aerator tubes 24 Granular filter media 25, 27 Fine stones, etc. 26 Granular activated carbon 51 Filtration chamber

Claims (1)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】 上下面が閉じられた密閉箱形状で、内部
がそれぞれ縦に配置した多孔材によって導水室、濾過
室、空室、活性炭室及び排水室に仕切られ、さらに前記
導水室及び濾過室が、それぞれの略中央部に設けた隔壁
によって二分割され、該二分割された導水室の二つの部
屋にはそれぞれ導水口が設けられ、上面にはそれぞれ逆
洗水排出口が設けられ、前記分割された濾過室の二つの
部屋内には下部にそれぞれ散気管が設けられるとともに
それぞれ濾材が充填され、さらに前記活性炭室には粒状
活性炭が充填され、前記排水室には処理水排出口が設け
られてなることを特徴とする活性炭水処理槽。
1. A closed box shape having upper and lower surfaces closed, and the inside is partitioned into a water guide chamber, a filtration chamber, an empty chamber, an activated carbon chamber, and a drain chamber by a vertically arranged porous material. The chamber is divided into two by a partition provided at a substantially central portion of each of the two, and the two divided water guide chambers are respectively provided with a water inlet, and the upper surface is provided with a backwash water outlet, respectively. A diffuser tube is provided at the bottom of each of the two divided filtration chambers, and a filter medium is filled therein.Furthermore, the activated carbon chamber is filled with granular activated carbon, and the drainage chamber has a treated water discharge port. An activated carbon water treatment tank, which is provided.
JP1992049127U 1992-06-19 1992-06-19 Activated carbon water treatment tank Expired - Fee Related JP2573454Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1992049127U JP2573454Y2 (en) 1992-06-19 1992-06-19 Activated carbon water treatment tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1992049127U JP2573454Y2 (en) 1992-06-19 1992-06-19 Activated carbon water treatment tank

Publications (2)

Publication Number Publication Date
JPH063484U JPH063484U (en) 1994-01-18
JP2573454Y2 true JP2573454Y2 (en) 1998-05-28

Family

ID=12822405

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1992049127U Expired - Fee Related JP2573454Y2 (en) 1992-06-19 1992-06-19 Activated carbon water treatment tank

Country Status (1)

Country Link
JP (1) JP2573454Y2 (en)

Also Published As

Publication number Publication date
JPH063484U (en) 1994-01-18

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