JPH0947616A - Active carbon filter - Google Patents

Active carbon filter

Info

Publication number
JPH0947616A
JPH0947616A JP22461595A JP22461595A JPH0947616A JP H0947616 A JPH0947616 A JP H0947616A JP 22461595 A JP22461595 A JP 22461595A JP 22461595 A JP22461595 A JP 22461595A JP H0947616 A JPH0947616 A JP H0947616A
Authority
JP
Japan
Prior art keywords
activated carbon
filter
active carbon
water
electrode
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
JP22461595A
Other languages
Japanese (ja)
Inventor
溥之 ▲高▼川
Hiroyuki Takagawa
Hiroo Ishida
博夫 石田
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.)
Churyo Engineering Co Ltd
Original Assignee
Churyo Engineering Co 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 Churyo Engineering Co Ltd filed Critical Churyo Engineering Co Ltd
Priority to JP22461595A priority Critical patent/JPH0947616A/en
Publication of JPH0947616A publication Critical patent/JPH0947616A/en
Pending legal-status Critical Current

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  • Water Treatment By Sorption (AREA)

Abstract

PROBLEM TO BE SOLVED: To simply and easily regenerate active carbon in an active carbon filter which can be used for treating clean water. SOLUTION: An active carbon layer 9 is formed on an electrode 8A and when an electric voltage is applied on the electrode 8A, the temp. of the active carbon is elevated and the pollutants adsorbed on the active carbon are changed to ashes. Then, the ashes are washed by feeding cleaning water through an inlet 4a and an outlet 5a for the water to be treated to regenerate the active carbon.

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】本発明は浄水の処理等に利用
できる活性炭瀘過器であって、活性炭の再生に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an activated carbon filter which can be used for treating purified water and the like, and relates to regeneration of activated carbon.

【0002】[0002]

【従来の技術】活性炭瀘過器は、浄水処理で除去できな
い異臭味、フェノール類、その他の有機物の除去に利用
している。図4(A)は従来の瀘過器100の概念図で
あり、その瀘過器100は、円筒状の外筒103と処理
水の入口104aを形成の上蓋104及び浄化された浄
化水の出口105aを形成の下蓋105とで、密閉容器
を形成する。又、前記外筒103内には間座107で一
定間隔を保った金網108を上下に設置し、その間に瀘
材として粒状の活性炭109aを充填して活性炭層10
9を形成する。そして、ポンプ110を介して送られて
来る処理水は、入口104aから入って、瀘材の活性炭
層109を通過することによって不純物が除去され、浄
化水となって出口105aから排出する。
2. Description of the Related Art Activated carbon filters are used to remove off-flavors, phenols and other organic substances that cannot be removed by water purification. FIG. 4 (A) is a conceptual diagram of a conventional filter 100, which is a cylindrical outer cylinder 103 and an upper lid 104 forming an inlet 104a of treated water and an outlet of purified purified water. A closed container is formed with the lower lid 105 forming 105a. In the outer cylinder 103, wire meshes 108, which are spaced by spacers 107 at regular intervals, are installed up and down, and granular activated carbon 109a as a filter is filled between them to activate the activated carbon layer 10
9 is formed. Then, the treated water sent through the pump 110 enters from the inlet 104a, passes through the activated carbon layer 109 of the filter material to remove impurities, becomes purified water, and is discharged from the outlet 105a.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、処理水
が多くなってくると、活性炭109aに吸着の汚濁物質
量が多くなって目詰まりが発生し、処理量が減少するた
め、活性炭109aの交換が必要となってくる。そこ
で、図4(B)に示すように、ポンプ110からの処理
水は複数設置の瀘過器100(100a、100b、1
00c)を介して行うが、それらの瀘過器100のう
ち、1又は2基は交換用瀘過器として配列してある。次
に、ポンプ110からの処理水を瀘過器100b、10
0cを介して瀘過中に、瀘過器100aを交換する操作
について具体的に説明すると、バルブ110aとバルブ
110bを閉とし、バルブ121を開、バルブ122を
閉、バルブ111a、111b及び112a、112b
を開、バルブ123を閉とする。処理水は瀘過器100
b、100cで処理されるが、瀘過器100aへの処理
水が遮断されて、交換が可能となる。この様に、瀘過器
100を複数台設置すると共に、瀘過器を停止して活性
炭の取替えを行う必要があり、その作業は手間暇がかか
る。尚、活性炭の再生処理は、通常100℃で乾燥した
後、焼成炉(400〜700℃)で再生処理を行ってい
るため、前記図4(B)の処理系統では、予備の活性炭
を用意しておく必要がある。そこで、本発明は、前記従
来とは異なる簡便な活性炭の再生を可能とする瀘過器を
提要するものである。
However, when the amount of treated water increases, the amount of pollutants adsorbed on the activated carbon 109a increases and clogging occurs, and the treated amount decreases. Therefore, it is necessary to replace the activated carbon 109a. Will be needed. Therefore, as shown in FIG. 4B, the treated water from the pump 110 is filtered by a plurality of filters 100 (100a, 100b, 1).
00c), one or two of the filters 100 are arranged as a replacement filter. Next, the treated water from the pump 110 is passed through the filters 100b, 10b.
The operation of exchanging the filter 100a during filtration through 0c will be specifically described. The valves 110a and 110b are closed, the valve 121 is opened, the valve 122 is closed, and the valves 111a, 111b and 112a, 112b
Is opened and the valve 123 is closed. Treated water is 100
Although the water is treated with b and 100c, the treated water to the filter 100a is shut off and can be replaced. In this way, it is necessary to install a plurality of filter devices 100 and stop the filter devices to replace the activated carbon, which requires time and effort. In addition, since the regeneration treatment of the activated carbon is usually performed at 100 ° C. and then in the firing furnace (400 to 700 ° C.), a preliminary activated carbon is prepared in the treatment system of FIG. 4 (B). Need to be kept. Therefore, the present invention requires a filter device that enables a simpler regeneration of activated carbon, which is different from the conventional one.

【0004】[0004]

【課題を解決するための手段】活性炭瀘過器に設けた電
極に電圧をかけると、水浸の活性炭層が抵抗となってジ
ュール熱が発生する。この熱で加熱された活性炭は、徐
々に昇温し、初めは水蒸気となって活性炭を乾燥する
が、その後、活性炭が高温になるにつれて活性炭に吸着
の汚濁物質が灰類に化す。その後、処理水の入口と出口
を介して洗浄水を送ると、前記灰類は洗浄されて、活性
炭は再生される。
When a voltage is applied to an electrode provided in an activated carbon filter, Joule heat is generated due to the activated carbon layer immersed in water becoming a resistance. The activated carbon heated by this heat gradually rises in temperature, and initially becomes steam to dry the activated carbon, but thereafter, as the activated carbon becomes hot, the pollutants adsorbed on the activated carbon turn into ash. After that, when washing water is sent through the treated water inlet and outlet, the ash is washed and the activated carbon is regenerated.

【0005】[0005]

【発明の実施の態様】DESCRIPTION OF THE PREFERRED EMBODIMENTS

(第1の発明の態様)図1(A)は瀘過器1を介して処
理水の瀘過状態、図1(B)は活性炭9の逆洗状態を示
す。円筒状で耐熱耐蝕性のセラミックス製の外筒3の上
開口には、処理水の入口4aを形成の上蓋4が脱着可能
に、又、外筒3の下開口には、浄化水の出口5aを形成
の下蓋5が脱着可能となっていて、瀘過器1の密閉容器
を形成する。尚、前記入口4a及び出口5aには、各
々、三方弁10、11が取り付けてある。又、前記外筒
3内には、絶縁性の間座7で一定間隔を保った金網状に
形成の耐熱耐蝕性のチタン電極8Aが上下に設置され、
その間に瀘材として活性炭9aを充填の活性炭層9を形
成する。又、前記電極8Aは、活性炭層9の水浸状態に
よる抵抗変化に対応可能に電圧電流値を変更可能な電圧
電流調整器12にリード線13を介して結線してあり、
前記電圧電流調整器12は交流電源14から供給を受け
る。
(Aspect of the First Invention) FIG. 1 (A) shows a filtered state of treated water through a filter 1, and FIG. 1 (B) shows a backwashed state of activated carbon 9. An upper lid 4 forming a treatment water inlet 4a is detachably attached to the upper opening of the cylindrical, heat- and corrosion-resistant ceramic outer cylinder 3, and an outlet 5a of purified water is attached to the lower opening of the outer cylinder 3. The lower lid 5 for forming the filter is detachable and forms a closed container of the filter 1. Three-way valves 10 and 11 are attached to the inlet 4a and the outlet 5a, respectively. Further, in the outer cylinder 3, there are vertically arranged heat-corrosion-resistant titanium electrodes 8A formed in a wire mesh shape with insulating spacers 7 at regular intervals.
In the meantime, an activated carbon layer 9 filled with activated carbon 9a as a filter is formed. Further, the electrode 8A is connected via a lead wire 13 to a voltage / current regulator 12 capable of changing the voltage / current value so as to correspond to the resistance change due to the water immersion state of the activated carbon layer 9,
The voltage / current regulator 12 is supplied from an AC power supply 14.

【0006】次に、図1(A)、図1(B)を参照して
の活性炭の再生について説明する。図1(A)に示す状
態は、処理水を活性炭層9で処理している状態を示し、
バルブ10及びバルブ11を図1(A)に示す位置とす
る。供給ポンプ20aから送られる処理水は、バルブ1
0を介して入口4aに流入し、金網状の電極8Aから活
性炭層9内に流れ込み、異臭味、フェノール類、その他
の有機物が活性炭9aに吸着し、浄化された浄化水は、
出口5a、バルブ11から排出する。
Next, the regeneration of activated carbon will be described with reference to FIGS. 1 (A) and 1 (B). The state shown in FIG. 1 (A) shows a state in which treated water is treated by the activated carbon layer 9,
The valve 10 and the valve 11 are set to the positions shown in FIG. The treated water sent from the supply pump 20a is the valve 1
0 through 0 into the inlet 4a, flowing into the activated carbon layer 9 from the wire mesh electrode 8A, off-flavors, phenols and other organic substances are adsorbed on the activated carbon 9a, purified water purified,
It is discharged from the outlet 5a and the valve 11.

【0007】そして、活性炭9aに多くの不純物が吸着
して、除去能力が低下したときには、前記バルブ10、
11を共に閉状態とし、処理水の処理を中止する。そし
て、電圧電流調整器12を起動させると、電極8A間に
電流が流れ、水浸の活性炭層9が抵抗となってジュール
熱が発生する。この熱で加熱された活性炭層9は、徐々
に昇温し、初めは水蒸気となって活性炭9aを乾燥する
が、その後、活性炭9aが高温になるにつれて活性炭9
aに吸着の汚濁物質が灰類に化す。尚、この間、バルブ
10又は別の図示しないバルブを開いて、水蒸気や脱気
ガスの放出を行う。そして、逆洗ポンプ20bから出口
5aを介して洗浄水を送ると、前記灰類は洗浄水と共に
入口4aから排出され、活性炭9aは再生されて、図1
(A)に示す状態で処理水の瀘過ができる。以上の様
に、処理水は、活性炭9aを介して瀘過ができるととも
に、所定時間、電極8Aに電流を流した後に、洗浄作業
をすることによって活性炭9aの再生ができて、再度、
処理が可能となる。
When a large amount of impurities are adsorbed on the activated carbon 9a and the removal ability is lowered, the valve 10,
Both 11 are closed and the treatment of the treated water is stopped. When the voltage / current regulator 12 is activated, a current flows between the electrodes 8A, and the activated carbon layer 9 immersed in water acts as a resistance to generate Joule heat. The activated carbon layer 9 heated by this heat gradually rises in temperature, and initially becomes steam to dry the activated carbon 9a, but thereafter, as the activated carbon 9a becomes higher in temperature, the activated carbon 9a is heated.
The pollutants adsorbed on a turn into ash. During this time, the valve 10 or another valve (not shown) is opened to release water vapor or degassed gas. Then, when washing water is sent from the backwash pump 20b through the outlet 5a, the ash is discharged together with the washing water from the inlet 4a, and the activated carbon 9a is regenerated.
The treated water can be filtered in the state shown in (A). As described above, the treated water can be filtered through the activated carbon 9a, and after the electric current is passed through the electrode 8A for a predetermined time, the activated carbon 9a can be regenerated by performing the washing work, and the
Processing becomes possible.

【0008】(第2の発明の態様)本実施の態様は、図
1(A)とは、電極8Aの位置を異にする構成であり、
図1(A)と同じ部品には同じ符号を附して説明を略
す。外筒3内の上下位置には、間座7で一定間隔を保っ
た金網8が設置してあり、その間に瀘材として活性炭9
が充填してある。又、耐熱耐蝕性の電極8Bは外筒3内
の左右端に設置してあり、電圧電流調整器12からのリ
ード線13に結線してある。この様に瀘過器を構成する
こともでき、処理水の処理及び活性炭9aの再生は前記
実施の態様1と同じであるため説明を略する。
(Second Aspect of the Invention) The present embodiment has a configuration in which the position of the electrode 8A is different from that of FIG. 1A.
The same parts as those in FIG. 1A are designated by the same reference numerals and the description thereof is omitted. Wire meshes 8 are installed at upper and lower positions in the outer cylinder 3 at regular intervals by spacers 7, and activated carbon 9 is used as a filter between them.
Is filled. Further, the heat and corrosion resistant electrodes 8B are installed at the left and right ends in the outer cylinder 3 and are connected to the lead wires 13 from the voltage / current regulator 12. The filter can be configured in this manner, and the treatment of the treated water and the regeneration of the activated carbon 9a are the same as those in the first embodiment, and therefore the description thereof is omitted.

【0009】(第3の発明の態様)本実施の態様は、図
1に示す瀘過器1を2台(1L、1R)併設し、交互の
使用を可能に構成するものであて、図1と同じ作用を示
す部品には同じ符号を附して、説明を略す。電極8Aへ
のリード線の途中には、連動切換えスイッチ2(2a、
2b)が配設してあり、何れか一方の電極8Aに導通す
る。そして、図3に示す状態は、ポンプ20aから処理
水をバルブ10、入口4a、活性炭層9、出口5a、バ
ルブ1を介して、瀘過器1Lで処理水を処理している状
態である。一方の瀘過器1Rは、電圧電流調整器12で
活性炭9aに吸着の不純物を灰類に化し、その状態とな
った後に、ポンプ20bから出口5aを介して洗浄水を
送って前記灰類を洗浄水と共に入口4aから排出して活
性炭を再生させる。本実施の態様のように、2基の瀘過
器1L、1Rを設置することによって、処理水の処理を
行っている瀘過器1Lに対して、もう一方の瀘過器1R
では、活性炭の再生を行うことができて、処理水の連続
操業が可能である。
(Third Aspect of the Invention) In the present embodiment, two filter devices 1 (1L, 1R) shown in FIG. 1 are provided side by side so that they can be alternately used. The same reference numerals are given to parts having the same operation as, and the description thereof will be omitted. In the middle of the lead wire to the electrode 8A, the interlocking changeover switch 2 (2a,
2b) is provided and conducts to either one of the electrodes 8A. The state shown in FIG. 3 is a state in which the treated water is treated from the pump 20a through the valve 10, the inlet 4a, the activated carbon layer 9, the outlet 5a, and the valve 1 by the filter 1L. On the other hand, the filter 1R converts impurities adsorbed on the activated carbon 9a into ash by the voltage / current regulator 12, and after this state is reached, washing water is sent from the pump 20b through the outlet 5a to remove the ash. The activated carbon is regenerated by discharging it through the inlet 4a together with the washing water. By installing the two filters 1L and 1R as in the present embodiment, the other filters 1R that are processing the treated water can be treated against the other filters 1R.
The activated carbon can be regenerated and the treated water can be continuously operated.

【0010】[0010]

【発明の効果】本発明は、電極を設けることによって活
性炭の再生が可能となり、従来と異なって、活性炭の入
れ替え作業を無くすることができる。
Industrial Applicability According to the present invention, it is possible to regenerate the activated carbon by providing the electrode, and unlike the conventional method, the replacement work of the activated carbon can be eliminated.

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

【図1】第1実施の態様の瀘過器の概念図である。FIG. 1 is a conceptual diagram of a filter according to a first embodiment.

【図2】第2実施の態様の瀘過器の概念図である。FIG. 2 is a conceptual diagram of a filter according to a second embodiment.

【図3】第3実施の態様の瀘過器の概念図である。FIG. 3 is a conceptual diagram of a filter according to a third embodiment.

【図4】従来の瀘過器の概念図である。FIG. 4 is a conceptual diagram of a conventional filter.

【符号の説明】[Explanation of symbols]

1 瀘過器 1L、1R 瀘過器 8A、8B 電極 9 活性炭層 9a 活性炭 10、11 三方バルブ 12 電圧電流調整器 20a 供給ポンプ 20b 逆洗ポンプ 1 Filter 1L, 1R Filter 8A, 8B Electrode 9 Activated carbon layer 9a Activated carbon 10, 11 Three-way valve 12 Voltage / current regulator 20a Supply pump 20b Backwash pump

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 処理水を入口から活性炭層に導き、その
活性炭層からの浄化水を出口から排出する活性炭瀘過器
において、前記活性炭層に電極を設け、その電極に電圧
をかけた後に、前記入口と出口を介して前記活性炭層の
洗浄を行うことを特徴とする活性炭瀘過器。
1. An activated carbon filter for introducing treated water from an inlet to an activated carbon layer and discharging purified water from the activated carbon layer from an outlet, after providing an electrode on the activated carbon layer and applying a voltage to the electrode, An activated carbon filter characterized in that the activated carbon layer is washed through the inlet and the outlet.
JP22461595A 1995-08-08 1995-08-08 Active carbon filter Pending JPH0947616A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22461595A JPH0947616A (en) 1995-08-08 1995-08-08 Active carbon filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22461595A JPH0947616A (en) 1995-08-08 1995-08-08 Active carbon filter

Publications (1)

Publication Number Publication Date
JPH0947616A true JPH0947616A (en) 1997-02-18

Family

ID=16816498

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22461595A Pending JPH0947616A (en) 1995-08-08 1995-08-08 Active carbon filter

Country Status (1)

Country Link
JP (1) JPH0947616A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100802365B1 (en) * 2006-09-29 2008-02-13 박대원 Activated carbon-granule electrode filter

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100802365B1 (en) * 2006-09-29 2008-02-13 박대원 Activated carbon-granule electrode filter
WO2008038853A1 (en) * 2006-09-29 2008-04-03 Dae Won Pak Activated carbon - granule electrode filter

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