JPH06254542A - Activated carbon filter device - Google Patents

Activated carbon filter device

Info

Publication number
JPH06254542A
JPH06254542A JP6749593A JP6749593A JPH06254542A JP H06254542 A JPH06254542 A JP H06254542A JP 6749593 A JP6749593 A JP 6749593A JP 6749593 A JP6749593 A JP 6749593A JP H06254542 A JPH06254542 A JP H06254542A
Authority
JP
Japan
Prior art keywords
activated carbon
carrier
water
layer
carrier layer
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
JP6749593A
Other languages
Japanese (ja)
Inventor
Keiko Miyamori
啓子 宮森
Masato Onishi
真人 大西
Naoki Okuma
直紀 大熊
Yutaka Okuno
裕 奥野
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.)
Hitachi Plant Technologies Ltd
Original Assignee
Hitachi Plant Technologies 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 Hitachi Plant Technologies Ltd filed Critical Hitachi Plant Technologies Ltd
Priority to JP6749593A priority Critical patent/JPH06254542A/en
Publication of JPH06254542A publication Critical patent/JPH06254542A/en
Pending legal-status Critical Current

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  • Water Treatment By Sorption (AREA)

Abstract

PURPOSE:To provide an activated carbon filter device capable of prolonging filtering duration and lessening the quantity of water for back-washing. CONSTITUTION:In the activated carbon filter device for purifying an original water for purified water containing a suspended solid after flocculating and settling, the activated carbon filter, device having a two bed structure composed of a carrier bed 12 made of a carrier having smaller specific gravity than activated carbon and an activated carbon bed 14 arranged in the lower step thereof are provided in a treating tank 10.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は活性炭により流入水中の
微量有機物、臭気成分などを除去するための活性炭濾過
装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an activated carbon filtration device for removing trace organic substances, odorous components, etc. in inflow water by activated carbon.

【0002】[0002]

【従来の技術】従来、固定槽で下向流の形式(上部から
被処理水を供給し、槽の下部から処理水を排出する方
式)の活性炭濾過装置は、装置内には活性炭のみを充填
した構成になっている。
2. Description of the Related Art Conventionally, an activated carbon filtering device of a fixed tank type having a downward flow (a system in which treated water is supplied from the upper part and treated water is discharged from the lower part of the tank) is filled with activated carbon only. It has been configured.

【0003】[0003]

【発明が解決しようとする課題】しかし、上記した従来
技術にあっては、充填物が活性炭のみであるため、流入
水(被処理水)の浮遊濁質が有る場合、これらが表層側
に蓄積しやすい。浮遊濁質が蓄積すると、目詰まりが生
じて水頭上昇速度が加速され、濾過継続時間が短くな
り、逆洗(活性炭層に対し、流入水の通過方向とは逆方
向から水洗用の水を供給する処理)頻度が多くなる。こ
の逆洗頻度が多くなることは逆洗水量も多くなるほか、
活性炭の磨耗も激しくなり、活性炭の充填密度の上昇を
招き、活性炭の圧力損失が高くなるという問題がある。
However, in the above-mentioned prior art, since the filling material is only activated carbon, if there is suspended turbidity of the inflow water (water to be treated), these accumulate on the surface side. It's easy to do. When suspended turbidity accumulates, clogging occurs, the head rising speed is accelerated, the duration of filtration is shortened, and backwashing (supplying water for washing to the activated carbon layer from the direction opposite to the inflowing water passage direction) Frequency). As the backwash frequency increases, the backwash water volume also increases,
There is also a problem that the wear of the activated carbon becomes severe, the packing density of the activated carbon increases, and the pressure loss of the activated carbon increases.

【0004】本発明の目的は、上記した従来技術の実情
に鑑みてなされたもので、濾過継続時間を長くできると
共に逆洗水量を少なくすることが可能な活性炭濾過装置
を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide an activated carbon filtration device which has been made in view of the above-mentioned circumstances of the prior art and which can increase the duration of filtration and reduce the amount of backwash water.

【0005】[0005]

【課題を解決するための手段】上記の目的を達成するた
めに、この発明は、浮遊濁質を含んだ浄水原水を活性炭
によって浄化する活性炭濾過装置において、前記活性炭
より比重の小さい担体からなる担体層と、前記担体層の
下段に配設された活性炭層と、を設けるようにしてい
る。
In order to achieve the above object, the present invention is an activated carbon filtration apparatus for purifying raw water for purified water containing suspended turbidity by activated carbon, the carrier comprising a carrier having a specific gravity smaller than that of the activated carbon. A layer and an activated carbon layer disposed below the carrier layer are provided.

【0006】[0006]

【作用】上記した手段によれば、活性炭層と、活性炭層
の上部に配置された活性炭よりも比重の軽い担体層との
2層構造にし、流入水中の浮遊濁質を主として担体層に
捕捉させ、活性炭層に流入する浮遊濁質を低減し、活性
炭層における逆洗水量を減少できるようにしている。こ
の結果、逆洗水量の減少、及び濾過継続時間の延長が可
能になる。
According to the above-mentioned means, the activated carbon layer and the carrier layer disposed above the activated carbon layer and having a lighter specific gravity than the activated carbon have a two-layer structure, and the suspended turbidity in the inflow water is mainly captured by the carrier layer. The amount of suspended turbidity flowing into the activated carbon layer is reduced and the amount of backwash water in the activated carbon layer can be reduced. As a result, it is possible to reduce the amount of backwash water and extend the duration of filtration.

【0007】[0007]

【実施例】図1は本発明による活性炭濾過装置の一実施
例を示す正面断面図であり、図2は図1に示す担体層の
逆洗水管部分の詳細を示す断面図である。
1 is a front sectional view showing an embodiment of an activated carbon filtration device according to the present invention, and FIG. 2 is a sectional view showing details of a backwash water pipe portion of a carrier layer shown in FIG.

【0008】上端が開口された処理水槽10の上部には
担体層12が配設され、その下部には活性炭層14が配
設されている。担体層12の素材は、活性炭層14より
も比重が軽く、かつ、活性炭の平均粒径と同等またはそ
れ以上の径の物質を用いている。担体層12に用いる担
体の材質としては、アンスサライト、プラスチックなど
を用いることができる。処理水槽10の底部には濾過後
の処理水18を取り出すための配管16が取り付けられ
ている。
A carrier layer 12 is disposed above the treated water tank 10 having an open upper end, and an activated carbon layer 14 is disposed below the carrier layer 12. The material of the carrier layer 12 is a material having a lower specific gravity than the activated carbon layer 14 and a diameter equal to or larger than the average particle diameter of the activated carbon. As the material of the carrier used for the carrier layer 12, anthsalite, plastic, or the like can be used. A pipe 16 for removing the filtered treated water 18 is attached to the bottom of the treated water tank 10.

【0009】また、担体層12の下面には逆洗を行うた
めのノズル20が設けられ、このノズル20には逆洗水
を供給するための逆洗水管22が接続されている。同様
に、活性炭層14の下部にはノズル24が配設され、こ
のノズル24には逆洗水管26が接続されている。
A nozzle 20 for backwashing is provided on the lower surface of the carrier layer 12, and a backwash water pipe 22 for supplying backwash water is connected to the nozzle 20. Similarly, a nozzle 24 is arranged below the activated carbon layer 14, and a backwash water pipe 26 is connected to the nozzle 24.

【0010】以上の構成において、処理水槽10の開口
部の上方からは、流入水28が供給され、担体層12を
通過する過程で流入水28中の浮遊濁質が捕捉され、つ
いで活性炭層14では担体層12で除去できなかった浮
遊濁質と該浮遊濁質以外の不純物などが除去され、洗浄
化された処理水18が配管16を通して取り出される。
そして、定期的または必要に応じてノズル20及びノズ
ル24に逆洗水が供給され、担体層12及び活性炭層1
4の洗浄が行われる。
In the above structure, inflow water 28 is supplied from above the opening of the treated water tank 10, and suspended turbidity in the inflow water 28 is captured in the process of passing through the carrier layer 12, and then the activated carbon layer 14 Then, suspended solids that could not be removed by the carrier layer 12 and impurities other than the suspended suspended solids are removed, and the treated water 18 that has been cleaned is taken out through the pipe 16.
Then, backwash water is supplied to the nozzle 20 and the nozzle 24 periodically or as needed, and the carrier layer 12 and the activated carbon layer 1
Washing 4 is performed.

【0011】図2に示すように、ノズル20は処理水槽
10の中心から放射状に延びるように配設されており、
抵抗を減らし、かつ活性炭よりも比重の低い担体層12
のみを逆洗することができ、逆洗水量の低減に寄与して
いる。また、担体層12の担体の平均粒径を活性炭の粒
径よりも大きくすることで、充填密度が低くなり、浮遊
濁質が担体層12中で捕捉され、表層で目詰まりを起こ
す場合よりも濾過継続時間が延長できるようになる。さ
らに、活性炭よりも比重の低い担体層12を主として逆
洗することから、活性炭層14の逆洗回数が減少し、活
性炭の磨耗を防止することができる。
As shown in FIG. 2, the nozzles 20 are arranged so as to extend radially from the center of the treated water tank 10.
Carrier layer 12 that reduces resistance and has a lower specific gravity than activated carbon
Only the backwash can be backwashed, which contributes to the reduction of the backwash water amount. Further, by making the average particle size of the carrier of the carrier layer 12 larger than the particle size of the activated carbon, the packing density becomes lower, and suspended turbidity is trapped in the carrier layer 12 than when the surface layer is clogged. The filtration duration can be extended. Further, since the carrier layer 12 having a specific gravity lower than that of activated carbon is mainly backwashed, the number of times of backwashing the activated carbon layer 14 is reduced, and abrasion of the activated carbon can be prevented.

【0012】図3は本発明の他の実施例を示す正面断面
図である。なお、図3においては、図1に用いたと同一
であるものには同一引用数字を用いたので、以下におい
ては重複する説明を省略する。
FIG. 3 is a front sectional view showing another embodiment of the present invention. Note that, in FIG. 3, the same reference numerals are used for the same elements as those used in FIG. 1, and thus duplicated description will be omitted below.

【0013】本実施例が前記実施例と異なるところは、
逆洗水管22の途中に逆洗空気管30を設けたところに
特徴がある。逆洗空気管30を設けたことにより、逆洗
水と逆洗用空気とを同時にノズル20に供給することが
できる。これにより、担体層12が硬質の場合、空気逆
洗によって濁質が担体を磨耗させることなく剥離され、
濾過継続時間を更に延長させることができる。
This embodiment is different from the above embodiment in that
A characteristic is that a backwash air pipe 30 is provided in the middle of the backwash water pipe 22. By providing the backwash air pipe 30, backwash water and backwash air can be supplied to the nozzle 20 at the same time. Thereby, when the carrier layer 12 is hard, the suspended matter is peeled off by backwashing with air without abrading the carrier,
The filtration duration can be further extended.

【0014】次に、本発明の実施結果について説明す
る。ここでは、図1の構成を用い、河川凝沈処理水を流
入水28として通水した。実験装置は、径300mmのカ
ラムを用いている。この結果は、表1(材質と担体及び
活性炭性状の関係を示す表)及び表2(実験条件を示す
表)の如くであり、従来の水頭上昇速度4cm/hに対し、
本発明では3cm/hとなり、濾過継続時間が延長されてい
ることがわかる。また、処理水質にも差は見られない。
Next, the results of carrying out the present invention will be described. Here, using the configuration of FIG. 1, the river coagulation treated water was passed as the inflow water 28. The experimental apparatus uses a column having a diameter of 300 mm. The results are as shown in Table 1 (a table showing the relationship between the material, the carrier and the properties of the activated carbon) and Table 2 (a table showing the experimental conditions), where the conventional head rising speed was 4 cm / h.
In the present invention, it is 3 cm / h, which shows that the filtration duration time is extended. In addition, there is no difference in the quality of treated water.

【0015】[0015]

【表1】 [Table 1]

【0016】[0016]

【表2】 [Table 2]

【0017】[0017]

【発明の効果】以上説明した通り、本発明は、浮遊濁質
を含んだ浄水原水を活性炭によって浄化する活性炭濾過
装置において、活性炭より比重の小さい担体からなる担
体層と、この担体層の下段に配設された活性炭層との2
層構造にしたので、逆洗水量の減少ほか、濾過継続時間
の延長が可能になる、という効果が得られる。
INDUSTRIAL APPLICABILITY As described above, according to the present invention, in an activated carbon filtration device for purifying purified water containing suspended solids by activated carbon, a carrier layer made of a carrier having a specific gravity smaller than that of activated carbon and a lower layer of the carrier layer are provided. 2 with the activated carbon layer arranged
Since it has a layered structure, it is possible to reduce the amount of backwash water and to extend the duration of filtration.

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

【図1】本発明による活性炭濾過装置の一実施例を示す
正面断面図である。
FIG. 1 is a front sectional view showing an embodiment of an activated carbon filtration device according to the present invention.

【図2】図1に示す担体層の逆洗水管部分の詳細を示す
断面図である。
FIG. 2 is a cross-sectional view showing details of a backwash water pipe portion of the carrier layer shown in FIG.

【図3】本発明の他の実施例を示す正面断面図である。FIG. 3 is a front sectional view showing another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10 処理水槽 12 担体層 14 活性炭層 16 配管 18 処理水 20、24 ノズル 26 逆洗水管 28 流入水 30 逆洗空気管 10 Treated Water Tank 12 Carrier Layer 14 Activated Carbon Layer 16 Piping 18 Treated Water 20, 24 Nozzle 26 Backwash Water Pipe 28 Inflow Water 30 Backwash Air Pipe

───────────────────────────────────────────────────── フロントページの続き (72)発明者 奥野 裕 東京都千代田区内神田1丁目1番14号 日 立プラント建設株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Yutaka Okuno 1-1-14 Kanda, Uchida, Chiyoda-ku, Tokyo Inside Hirit Plant Construction Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 浮遊濁質を含んだ浄水原水を活性炭によ
って浄化する活性炭濾過装置において、前記活性炭より
比重の小さい担体からなる担体層と、前記担体層の下段
に配設された活性炭層と、を設けたことを特徴とする活
性炭濾過装置。
1. An activated carbon filtration apparatus for purifying purified water containing suspended solids by activated carbon, comprising: a carrier layer made of a carrier having a specific gravity smaller than that of the activated carbon; and an activated carbon layer disposed below the carrier layer. An activated carbon filtration device characterized by being provided with.
JP6749593A 1993-03-03 1993-03-03 Activated carbon filter device Pending JPH06254542A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6749593A JPH06254542A (en) 1993-03-03 1993-03-03 Activated carbon filter device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6749593A JPH06254542A (en) 1993-03-03 1993-03-03 Activated carbon filter device

Publications (1)

Publication Number Publication Date
JPH06254542A true JPH06254542A (en) 1994-09-13

Family

ID=13346633

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6749593A Pending JPH06254542A (en) 1993-03-03 1993-03-03 Activated carbon filter device

Country Status (1)

Country Link
JP (1) JPH06254542A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006231285A (en) * 2005-02-28 2006-09-07 Toyo Constr Co Ltd Gravity filtration apparatus
WO2015046056A1 (en) * 2013-09-25 2015-04-02 三菱重工業株式会社 Biofilm filtration device and backwash method for biofilm filtration device
WO2020045411A1 (en) * 2018-08-30 2020-03-05 パナソニックIpマネジメント株式会社 Water treatment device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006231285A (en) * 2005-02-28 2006-09-07 Toyo Constr Co Ltd Gravity filtration apparatus
WO2015046056A1 (en) * 2013-09-25 2015-04-02 三菱重工業株式会社 Biofilm filtration device and backwash method for biofilm filtration device
JP2015062868A (en) * 2013-09-25 2015-04-09 三菱重工業株式会社 Biological membrane filter device and method for backwashing biological membrane filter device
AU2014325264B2 (en) * 2013-09-25 2017-08-31 Mitsubishi Heavy Industries Engineering, Ltd. Biofilm filtration device and backwash method for biofilm filtration device
WO2020045411A1 (en) * 2018-08-30 2020-03-05 パナソニックIpマネジメント株式会社 Water treatment device

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