JP2002273434A - Treating device and treating method for ionic substance- containing water using activated carbon electrode and regenerating method of activated carbon electrode - Google Patents

Treating device and treating method for ionic substance- containing water using activated carbon electrode and regenerating method of activated carbon electrode

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Publication number
JP2002273434A
JP2002273434A JP2001079075A JP2001079075A JP2002273434A JP 2002273434 A JP2002273434 A JP 2002273434A JP 2001079075 A JP2001079075 A JP 2001079075A JP 2001079075 A JP2001079075 A JP 2001079075A JP 2002273434 A JP2002273434 A JP 2002273434A
Authority
JP
Japan
Prior art keywords
activated carbon
solid activated
ionic substance
water
electrodes
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.)
Withdrawn
Application number
JP2001079075A
Other languages
Japanese (ja)
Inventor
Kazuhiro Baba
和宏 馬場
Takayuki Saito
貴之 齋藤
Masa Masuzawa
雅 鱒沢
Toru Suganuma
徹 菅沼
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.)
NEC Corp
NEC Ameniplantex Ltd
Original Assignee
NEC Corp
NEC Ameniplantex 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 NEC Corp, NEC Ameniplantex Ltd filed Critical NEC Corp
Priority to JP2001079075A priority Critical patent/JP2002273434A/en
Publication of JP2002273434A publication Critical patent/JP2002273434A/en
Withdrawn legal-status Critical Current

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  • Water Treatment By Electricity Or Magnetism (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method of treating an ionic substance-containing water using an activated carbon electrode which efficiently adsorbs ions which are included in water to be treated, conveniently and surely removes the ions which are adsorbed on electrodes and can regenerate the electrode, a regenerating method of the activated carbon electrode and a treating device for the ionic substance-containing water. SOLUTION: Solid activated carbon electrodes 1, 2 are disposed in a treating water vessel 6 and releasing electrodes 3, 4 for having no ionic adsorbability are disposed on both outer sides of the solid activated carbon electrodes and, in the electric double layer adsorption treatment, a direct current power source 7 is connected with the solid activated carbon electrode. In the regeneration of the solid activated carbon electrodes which adsorb an ionic substance, the ionic substance is released by short- circuiting between the solid activated carbon electrodes (8c-8d), thereafter, a direct current power source is connected with the releasing electrodes so as to invert the polarity, furthermore, the ionic substance is moved from the solid activated carbon electrodes and the solid activated carbon electrodes are thus surely regenerated with a simple structure.

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、イオン性物質含有
水を電気的に浄化する方法および処理装置に関し、特
に、イオンを含む被処理水から高表面積を持つ固体活性
炭電極にイオン性物質を電気二重層吸着して浄化する方
法、該固体活性炭電極を再生する方法及びイオン性物質
含有水の処理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for electrically purifying ionic substance-containing water. More particularly, the present invention relates to a method for converting ionic substances from water to be treated containing ions to a solid activated carbon electrode having a high surface area. The present invention relates to a method for purifying by double-layer adsorption, a method for regenerating the solid activated carbon electrode, and an apparatus for treating ionic substance-containing water.

【0002】[0002]

【従来の技術】従来から、液中のイオン性物質を浄化す
る方法として、 1)逆浸透膜を使用して加圧濾過する方法、 2)電極間に多数のイオン交換膜を配し、電気泳動によ
りイオンを分離する電気透析法、 3)イオン交換樹脂に吸着する方法、 4)加熱して蒸留する方法、 などが知られている。
2. Description of the Related Art Conventionally, as a method for purifying ionic substances in a liquid, 1) a method of pressure filtration using a reverse osmosis membrane, 2) a large number of ion exchange membranes disposed between electrodes, There are known an electrodialysis method in which ions are separated by electrophoresis, 3) a method of adsorbing on an ion exchange resin, and 4) a method of heating and distilling.

【0003】しかし、これらの方法ではエネルギーを多
く消費するという問題や、膜や樹脂が高価であり洗浄や
再生の工程が複雑で薬品を必要とするという問題や、析
出した塩の付着や粒子状物質が原因となる目詰まり等に
弱いという問題があった。
[0003] However, these methods consume a large amount of energy, are expensive in membranes and resins, complicate washing and regeneration steps, and require chemicals. There is a problem that the material is vulnerable to clogging or the like caused by the substance.

【0004】上記問題を解決する方法として、電気二重
層によるイオン吸着が提案されている。例えば、特開平
5−258992号公報では、多数の高表面積導電層、
非導電層をスパイラル状に巻回した通液型コンデンサに
よる方法が示されている。また、特開平6−32598
3号公報では、非導電通液性シートを挟んで活性炭層を
配置し、その外側に集電極を配置した構成を有する平板
形状の通液型電気二重層コンデンサが示されている。
As a method for solving the above problem, ion adsorption by an electric double layer has been proposed. For example, in Japanese Patent Application Laid-Open No. H5-258992, a large number of high surface area conductive layers,
A method using a flow-through capacitor in which a non-conductive layer is spirally wound is shown. Also, Japanese Patent Application Laid-Open No. 6-32598
In JP-A No. 3 (1999) -1995, there is disclosed a plate-shaped liquid-flow type electric double-layer capacitor having a configuration in which an activated carbon layer is disposed with a non-conductive liquid-permeable sheet interposed therebetween and a collector electrode is disposed outside the activated carbon layer.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、これら
の方法ではいずれの場合も実用上問題がある。すなわ
ち、特開平5−258992号公報記載の方法では、装
置構造が複雑なスパイラル状であるため、通液時に偏流
を生じ易く能力が安定しないという問題がある。また、
特開平6−325983号公報の記載方法では、偏流の
改善は行われているが、両者の場合とも活性炭を再生す
る場合に、コンデンサを含む回路をショートさせながら
通液を行っているが、この方法では活性炭に吸着された
イオンを強制的に排出できず、イオンが残存してしまう
という問題がある。
However, these methods have practical problems in any case. That is, in the method described in Japanese Patent Application Laid-Open No. H5-258992, there is a problem in that since the device has a complicated spiral structure, drift is likely to occur when the liquid is passed and the ability is not stable. Also,
In the method described in JP-A-6-325983, the drift is improved, but in both cases, when the activated carbon is regenerated, the liquid is passed while the circuit including the capacitor is short-circuited. In the method, ions adsorbed on the activated carbon cannot be forcibly discharged, and there is a problem that ions remain.

【0006】活性炭中のイオンをより完全に放出する方
法としては、吸着時の回路の極性を反転させてコンデン
サを逆充電して電気的斥力により放出を行うことも考え
られるが、その際には逆充電開始直後から極性反転後の
対をなす活性炭にイオンの移動が始まり再び吸着される
ため、活性炭に吸着されたイオンの残存率は前記回路シ
ョートによる方法より大きくなってしまうという問題が
ある。また、両者の場合共に、イオン吸着量を増やすた
めに活性炭部の体積を増やしたり、複数の単位コンデン
サを含む構成にする等の処置が考えられるが、いずれの
場合も活性炭の電位を保つため電源が大型化してしま
う。
As a method of more completely releasing the ions in the activated carbon, it is conceivable to invert the polarity of the circuit at the time of adsorption and reversely charge the capacitor to release the ions by electric repulsion. Immediately after the start of the reverse charging, the ions start to move to the activated carbon of the pair after the polarity inversion, and are adsorbed again. Therefore, there is a problem that the residual ratio of the ions adsorbed to the activated carbon becomes larger than that of the method by the circuit short circuit. In both cases, measures such as increasing the volume of the activated carbon part in order to increase the amount of ion adsorption or using a configuration including a plurality of unit capacitors are conceivable. Becomes large.

【0007】本発明は、上記問題点に鑑みてなされたも
のであって、その主たる目的は、被処理水に含まれるイ
オンを効率よく吸着し、かつ、電極に吸着したイオンを
簡便かつ確実に除去して電極を再生することができる活
性炭電極を用いたイオン性物質含有水の処理方法及び該
活性炭電極の再生方法並びにイオン性物質含有水の処理
装置を提供することにある。
SUMMARY OF THE INVENTION The present invention has been made in view of the above problems, and has as its main object to efficiently and efficiently adsorb ions contained in water to be treated and to easily and reliably adsorb ions adsorbed on an electrode. An object of the present invention is to provide a method for treating ionic substance-containing water using an activated carbon electrode capable of removing and regenerating an electrode, a method for regenerating the activated carbon electrode, and a treatment apparatus for treating ionic substance-containing water.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するた
め、本発明のイオン性物質含有水の処理方法は、被処理
水に含まれるイオン性物質を電気二重層吸着して浄化す
る処理方法において、処理槽内に、1以上の対をなす固
体活性炭電極とイオン吸着能を持たない一対の放出用電
極とを備え、前記被処理水を処理するに際し、直流電源
を前記対をなす固体活性炭電極に接続して前記イオン性
物質を電気二重層吸着し、前記イオン性物質を吸着した
前記固体活性炭電極を再生するに際し、前記対をなす固
体活性炭電極を短絡させた後、前記直流電源を前記放出
用電極に接続して前記固体活性炭電極から前記イオン性
物質を放出させるものである。
In order to achieve the above object, a method for treating ionic substance-containing water according to the present invention is directed to a method for purifying an ionic substance contained in water to be treated by electric double layer adsorption. A treatment tank, comprising one or more pairs of solid activated carbon electrodes and a pair of discharge electrodes having no ion-adsorbing ability, and when treating the water to be treated, supplying a DC power supply to the pair of solid activated carbon electrodes. To connect the ionic substance to the electric double layer, and to regenerate the solid activated carbon electrode to which the ionic substance is adsorbed, after short-circuiting the pair of solid activated carbon electrodes, discharge the DC power supply. The ionic substance is released from the solid activated carbon electrode by connecting to an electrode for use.

【0009】本発明においては、前記固体活性炭電極が
活性炭/炭素複合材料を含み、前記活性炭が活性炭粉末
または活性炭繊維を含み、前記炭素複合材料がフェノー
ル樹脂の炭化物の複合材料を含むことが好ましい。
In the present invention, it is preferable that the solid activated carbon electrode contains an activated carbon / carbon composite material, the activated carbon contains activated carbon powder or activated carbon fiber, and the carbon composite material contains a phenolic carbide composite material.

【0010】また、本発明においては、前記固体活性炭
電極の再生に際し、前記イオン性物質が吸着された前記
被処理水を放流し、予め設けた再生用の水槽から前記処
理槽に再生用水を注入して前記固体活性炭電極の再生を
行い、再生が終了したら再び前記再生用水を前記再生用
水槽に移送する構成とすることができる。
In the present invention, when the solid activated carbon electrode is regenerated, the water to be treated having the ionic substance adsorbed thereon is discharged, and water for regeneration is injected into the treatment tank from a water tank for regeneration provided in advance. Then, the solid activated carbon electrode is regenerated, and when the regeneration is completed, the regenerating water is transferred to the regenerating water tank again.

【0011】また、本発明においては、前記一対の放出
用電極を前記対をなす固体活性炭電極の両外側に配設
し、かつ、電極の極性を前記放出用電極と前記固体活性
炭電極とで逆となるように設定する構成とすることがで
きる。
In the present invention, the pair of discharge electrodes are disposed on both outer sides of the pair of solid activated carbon electrodes, and the polarities of the electrodes are reversed between the discharge electrode and the solid activated carbon electrodes. It can be configured to be set so that

【0012】また、本発明においては、前記固体活性炭
電極の対を複数備え、各々の対を順次選択して前記直流
電源に接続して吸着処理を行う構成とすることもでき
る。
Further, in the present invention, a plurality of pairs of the solid activated carbon electrodes may be provided, and each pair may be sequentially selected and connected to the DC power supply to perform an adsorption process.

【0013】また、本発明のイオン性物質含有水の処理
装置は、被処理水中のイオン性物質を電気二重層吸着し
て浄化する処理装置において、処理槽と、1以上の対を
なす固体活性炭電極と、イオン吸着能を持たない一対の
放出用電極と、直流電源と、該直流電源と接続される電
極を選択する切り替え手段と、前記対をなす固体活性炭
電極を相互に短絡させる回路とを少なくとも有し、前記
被処理水を処理するに際し、前記直流電源と前記対をな
す固体活性炭電極とが接続されて前記イオン性物質が電
気二重層吸着され、前記イオン性物質を吸着した前記固
体活性炭電極を再生するに際し、前記短絡回路によって
前記対をなす固体活性炭電極が短絡され、前記切り替え
手段によって前記直流電源と前記放出用電極とが接続さ
れて前記固体活性炭電極から前記イオン性物質が放出さ
れるものである。
[0013] The treatment apparatus for ionic substance-containing water of the present invention is a treatment apparatus for purifying ionic substances in water to be treated by adsorbing an electric double layer, wherein the treatment tank and one or more pairs of solid activated carbon are formed. An electrode, a pair of discharge electrodes having no ion-adsorbing ability, a DC power supply, a switching unit for selecting an electrode connected to the DC power supply, and a circuit for short-circuiting the pair of solid activated carbon electrodes to each other. At least, when treating the water to be treated, the DC power source and the solid activated carbon electrode forming the pair are connected, the ionic substance is adsorbed by the electric double layer, and the solid activated carbon adsorbed by the ionic substance is When the electrodes are regenerated, the pair of solid activated carbon electrodes is short-circuited by the short circuit, and the switching means connects the DC power supply and the discharge electrode to form the solid active carbon electrode. The ionic material from the electrode is intended to be released.

【0014】すなわち、本発明は、上記課題を解決する
ために、固体活性炭を両極に用いた処理装置により被処
理水中のイオンを電気二重層吸着し、活性炭吸着が飽和
した際には固体活性炭電極を含む回路をショートさせ、
その後、固体活性炭電極の両外側に配置した放出用電極
に通電することにより、吸着したイオンを高い効率で放
出させ両極の固体活性炭を再生することを特徴とするも
のである。
That is, in order to solve the above-mentioned problems, the present invention provides an electric double layer adsorption of ions in the water to be treated by a treatment apparatus using solid activated carbon for both electrodes, and when the activated carbon adsorption is saturated, the solid activated carbon electrode is used. Short circuit including
Thereafter, by applying a current to the discharge electrodes arranged on both outer sides of the solid activated carbon electrode, the adsorbed ions are released with high efficiency to regenerate the solid activated carbon at both electrodes.

【0015】なお、固体活性炭を上記構成とすることに
より、体積あたりの吸着性能が粉末活性炭と同等以上の
薄板形状の固体活性炭電極を形成することができ、この
固体活性炭電極に直接通電して電界を発生させることが
できる。従って、高価で塩の析出等により閉塞する可能
性があるイオン交換膜等を用いることなく、水中のイオ
ンを吸着処理することができる。
By using the above-described solid activated carbon, it is possible to form a thin plate-shaped solid activated carbon electrode having an adsorption performance per volume equal to or higher than that of powdered activated carbon. Can be generated. Therefore, ions in water can be adsorbed without using an ion-exchange membrane or the like which is expensive and may be blocked due to salt precipitation or the like.

【0016】更に、イオン吸着量を増やすために複数の
単位コンデンサを設ける場合には、単位コンデンサを同
時では無く分割して通電することにより電源を大型化す
ることなく、イオンの吸着量を増やすことができる。
Further, when a plurality of unit capacitors are provided in order to increase the amount of ion adsorption, the unit capacitors are divided and not energized at the same time, so that the amount of ion adsorption can be increased without enlarging the power supply. Can be.

【0017】[0017]

【発明の実施の形態】本発明に係るイオン性物質含有水
の処理方法は、その好ましい一実施の形態において、処
理水槽内に、固体活性炭電極とその両外側にイオン吸着
能を持たない放出用電極とが設けられ、電気二重層吸着
処理に際しては、切り替えスイッチによって直流電源を
固体活性炭電極に接続し、イオン性物質を吸着した固体
活性炭電極の再生に際しては、固体活性炭電極間をショ
ートさせてイオン性物質を放出させた後、切り替えスイ
ッチによって直流電源を放出用電極に接続して固体活性
炭電極から更にイオン性物質を移動させるものであり、
簡単な構造で確実に固体活性炭電極の再生を可能とする
と共に、この吸着/再生を繰り返すことにより、固体活
性炭電極の吸着能を高く維持することができる。
BEST MODE FOR CARRYING OUT THE INVENTION In a preferred embodiment of the method for treating water containing ionic substances according to the present invention, a solid activated carbon electrode and a discharge electrode having no ion-adsorbing ability on both outer sides thereof are provided in a treatment water tank. An electrode is provided.In the electric double layer adsorption treatment, a DC power supply is connected to the solid activated carbon electrode by a changeover switch, and in the regeneration of the solid activated carbon electrode having adsorbed an ionic substance, the solid activated carbon electrode is short-circuited to ionize. After releasing the ionic substance, a DC power supply is connected to the discharge electrode by a changeover switch to further move the ionic substance from the solid activated carbon electrode,
The solid activated carbon electrode can be reliably regenerated with a simple structure, and the adsorption capacity of the solid activated carbon electrode can be maintained high by repeating this adsorption / regeneration.

【0018】[0018]

【実施例】上記した本発明の実施の形態についてさらに
詳細に説明すべく、本発明の実施例について図面を参照
して説明する。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a block diagram showing an embodiment of the present invention;

【0019】[実施例1]まず、本発明の第1の実施例
に係る固体活性炭電極を用いたイオン性物質含有水の処
理方法及び固体活性炭電極の再生方法並びにイオン性物
質含有水の処理装置について、図1を参照して説明す
る。図1は、本実施例に係るイオン性物質含有水の処理
装置の構造を模式的に示す断面図である。図1におい
て、1〜2は固体活性炭電極、3〜4は放出用電極、5
は被処理水、6は処理用水槽、7は直流電源、8a〜8
fは直流電源の回路の状態を切り替えるためのスイッチ
接点である。なお、被処理水5はイオンを含むものと
し、被処理水5を処理用水槽6内に注入し、イオン性物
質の電気二重層吸着脱塩処理を行うが、この手順につい
て以下に説明する。
Embodiment 1 First, a method for treating ionic substance-containing water using a solid activated carbon electrode, a method for regenerating a solid activated carbon electrode, and an apparatus for treating ionic substance-containing water according to a first embodiment of the present invention. Will be described with reference to FIG. FIG. 1 is a cross-sectional view schematically showing the structure of the ionic substance-containing water treatment apparatus according to the present embodiment. In FIG. 1, 1-2 are solid activated carbon electrodes, 3-4 are discharge electrodes,
Is the water to be treated, 6 is a treatment tank, 7 is a DC power supply, and 8a to 8a.
f is a switch contact for switching the state of the circuit of the DC power supply. In addition, the to-be-processed water 5 contains ions, the to-be-processed water 5 is injected into the treatment water tank 6, and the electric double layer adsorption and desalination treatment of the ionic substance is performed. This procedure will be described below.

【0020】まず、直流電源7には通電する電極を選択
するスイッチが接続されており、このスイッチを調整し
て回路接点8aと8c、8bと8dを接続させ、固体活
性炭電極1を陽極に、固体活性炭電極2を陰極として電
気二重層吸着を行う。すると、被処理水5に含まれてい
るアニオンの大部分は陽極(固体活性炭電極1)に、カ
チオンは陰極(固体活性炭電極2)に引き寄せられ、固
体活性炭の持つ優れた吸着性能により、アニオン及びカ
チオンは固体活性炭表面に吸着される。そして、被処理
水5に含まれるイオンを活性炭が飽和するまで吸着させ
た後、イオンの放出による固体活性炭電極の再生を行
う。
First, a switch for selecting an electrode to be energized is connected to the DC power source 7. The switch is adjusted to connect the circuit contacts 8a and 8c, 8b and 8d, and the solid activated carbon electrode 1 is used as an anode. Electric double layer adsorption is performed using the solid activated carbon electrode 2 as a cathode. Then, most of the anions contained in the water 5 to be treated are attracted to the anode (solid activated carbon electrode 1), and the cations are attracted to the cathode (solid activated carbon electrode 2). Cations are adsorbed on the surface of solid activated carbon. Then, after the ions contained in the water 5 to be treated are adsorbed until the activated carbon is saturated, the solid activated carbon electrode is regenerated by releasing the ions.

【0021】イオンの放出に際して、吸着処理済みの処
理水9は放流ライン10を通じて放流し、代わりに濃縮
用水槽13から濃縮用水移送ライン12を通して濃縮用
水11を注入する。次に、スイッチ接点8cと8dを接
続し、回路をショートさせて電気二重層コンデンサから
イオンを放出させ、固体活性炭電極1、2を電気的に中
性にする。その後、スイッチ接点8aと8e、8bと8
fを接続することにより、陽極(固体活性炭電極1)に
残存しているアニオン及び陰極(固体活性炭電極2)に
残存しているカチオンは、放出用電極3、4へ向けて移
動する。
Upon release of the ions, the treated water 9 having been subjected to the adsorption treatment is discharged through a discharge line 10, and instead, the concentrated water 11 is injected from a concentrated water tank 13 through a concentrated water transfer line 12. Next, the switch contacts 8c and 8d are connected, the circuit is short-circuited, ions are released from the electric double layer capacitor, and the solid activated carbon electrodes 1, 2 are made electrically neutral. Thereafter, the switch contacts 8a and 8e, 8b and 8
By connecting f, anions remaining on the anode (solid activated carbon electrode 1) and cations remaining on the cathode (solid activated carbon electrode 2) move toward the discharge electrodes 3, 4.

【0022】放出用電極3、4はイオン吸着能を持たな
い材料、例えば金属等で形成されているため、固体活性
炭電極1、2から放出されたイオンは水中に漂うことに
なり、濃縮用水11中のイオン濃度が増加して、固体活
性炭電極1、2に吸着されたイオンの量は減少する。そ
して、イオンの放出による固体活性炭電極1、2の再生
後、イオン濃度が増加した濃縮用水11は、濃縮用水移
送ライン12を通じて再び濃縮用水槽13に移送され
る。この後、同様の手順を濃縮用水11の塩濃度が過飽
和近くになるまで繰り返し、濃縮用水11の塩濃度が過
飽和近くになったら濃縮用水排出ライン14を通じて濃
縮用水11を排出する。
Since the discharge electrodes 3 and 4 are formed of a material having no ion-adsorbing ability, for example, a metal or the like, the ions discharged from the solid activated carbon electrodes 1 and 2 float in water, and the concentrated water 11 The ion concentration inside increases, and the amount of ions adsorbed on the solid activated carbon electrodes 1 and 2 decreases. After the regeneration of the solid activated carbon electrodes 1 and 2 by the release of ions, the concentrated water 11 having the increased ion concentration is transferred again to the concentrated water tank 13 through the concentrated water transfer line 12. Thereafter, the same procedure is repeated until the salt concentration of the concentrated water 11 becomes close to supersaturation. When the salt concentration of the concentrated water 11 becomes close to supersaturation, the concentrated water 11 is discharged through the concentrated water discharge line 14.

【0023】このように、本実施例のイオン性物質含有
水の処理方法及び固体活性炭電極の再生方法並びにイオ
ン性物質含有水の処理装置によれば、吸着イオンが飽和
するまで固体活性炭電極1、2に通電してアニオン及び
カチオンを電気二重層吸着させ、飽和したら処理用水槽
6に濃縮用水11を導入し、固体活性炭電極1、2間を
ショートさせて吸着したイオンを放出させると共に、固
体活性炭電極1、2の両外側に設けたイオン吸着能を持
たない放出用電極3、4に通電し、固体活性炭電極1、
2から更にイオンを移動させることにより、高効率で固
体活性炭電極を再生することができる。
As described above, according to the method for treating ionic substance-containing water, the method for regenerating a solid activated carbon electrode, and the apparatus for treating ionic substance-containing water according to the present embodiment, the solid activated carbon electrode 1 until the adsorbed ions are saturated. 2, the anion and the cation are adsorbed in the electric double layer, and when saturated, the condensed water 11 is introduced into the treatment tank 6 to short-circuit the solid activated carbon electrodes 1 and 2 to release the adsorbed ions and to release the solid activated carbon. Electricity is supplied to the discharge electrodes 3 and 4 having no ion-adsorbing ability provided on both outer sides of the electrodes 1 and 2 so that the solid activated carbon electrodes 1 and
By further moving ions from 2, the solid activated carbon electrode can be regenerated with high efficiency.

【0024】なお、固体活性炭電極1、2及び放出用電
極3、4の配置は図の構成に限定されるものではなく、
電極の極性は反転しても良く、また、固体活性炭電極の
間や固体活性炭電極対に直交する方向(例えば、固体活
性炭電極が図の左右方向に対向している場合は紙面に直
交する方向)に配置しても良い。また、吸着と放出に際
して供給する電圧は同じでも異なっていても良い。
The arrangement of the solid activated carbon electrodes 1 and 2 and the discharge electrodes 3 and 4 is not limited to the configuration shown in FIG.
The polarity of the electrodes may be reversed, and between the solid activated carbon electrodes or in a direction orthogonal to the pair of solid activated carbon electrodes (for example, in a case where the solid activated carbon electrodes are opposed to the left and right directions in the drawing, the direction orthogonal to the paper surface). May be arranged. Further, the voltages supplied during adsorption and release may be the same or different.

【0025】更に、固体活性炭電極1、2の短絡及び直
流電源7の接続の切り替えは手動で行っても良いが、処
理用水槽6に濃縮用水11のイオン濃度を検出するセン
サを設置し、センサからの出力に連動させて自動的に接
続の切替を行うような構成としても良い。
Further, the short-circuiting of the solid activated carbon electrodes 1 and 2 and the switching of the connection of the DC power source 7 may be performed manually, but a sensor for detecting the ion concentration of the condensed water 11 is installed in the water tank 6 for treatment. It is also possible to adopt a configuration in which the connection is automatically switched in conjunction with the output from the server.

【0026】[実施例2]次に、本発明の第2の実施例
に係る固体活性炭電極を用いたイオン性物質含有水の処
理方法及び処理装置について、図2を参照して説明す
る。図2は、固体活性炭によるイオン性物質吸着法にお
いて、イオンの吸着能を高めるために、装置に複数のコ
ンデンサを設けた場合の構造を示す断面図である。
Embodiment 2 Next, a method and an apparatus for treating ionic substance-containing water using a solid activated carbon electrode according to a second embodiment of the present invention will be described with reference to FIG. FIG. 2 is a cross-sectional view showing a structure in which a plurality of capacitors are provided in the device in order to enhance the ability to adsorb ions in the ionic substance adsorption method using solid activated carbon.

【0027】図2において、15は固体活性炭電極コン
デンサユニット、16は直流電源、17は電源−スイッ
チ接点(aは陽極用、bは陰極用)であり、接点を中心
にスイッチはスイッチ盤上を回転する。また、18はス
イッチ盤(aは陽極用、bは陰極用)、19はスイッチ
(aは陽極用、bは陰極用)、20a〜20dは固体活
性炭電極コンデンサユニット−スイッチ接点で、破線の
先で固体活性炭電極コンデンサユニット15と接続して
いる。また、21は処理水槽、22は被処理水である。
In FIG. 2, 15 is a solid activated carbon electrode capacitor unit, 16 is a DC power supply, 17 is a power-switch contact (a is for an anode, and b is for a cathode). Rotate. Reference numeral 18 denotes a switch panel (a is for an anode, b is for a cathode), 19 is a switch (a is for an anode, b is for a cathode), 20a to 20d are solid activated carbon electrode capacitor unit-switch contacts, and the end of the broken line Is connected to the solid activated carbon electrode capacitor unit 15. 21 is a treated water tank and 22 is water to be treated.

【0028】被処理水22を処理水槽21内に注入し、
イオン性物質の電気二重層吸着脱塩処理を行うが、その
際スイッチ19a、19bは、それぞれ隣同士で対にな
って構成されている固体活性炭電極に繋がる固体活性炭
電極コンデンサユニット−スイッチ接点20a、20b
に接続されるよう、電源−スイッチ接点17a、17b
を中心にスイッチ盤18a、18b上を回転させる。
The to-be-treated water 22 is poured into the treated water tank 21,
The electric double layer adsorption and desalination treatment of the ionic substance is performed. At this time, the switches 19a and 19b are connected to the solid activated carbon electrode formed adjacently in pairs and connected to the solid activated carbon electrode capacitor unit-switch contact 20a, 20b
Power supply-switch contacts 17a, 17b
Are rotated on the switch boards 18a and 18b.

【0029】そして、1つの固体活性炭電極コンデンサ
ユニット15が飽和したら、スイッチ19a、19bが
他の固体活性炭電極コンデンサユニット−スイッチ接点
20c、20dに接続されるように順次切り替えてい
く。その際、直流電源16から解放された固体活性炭電
極コンデンサユニット−スイッチ接点20a、20bに
繋がる固体活性炭電極コンデンサユニット15は、電気
二重層にイオンの吸着を保ち続ける。同様の操作を全て
の固体活性炭電極コンデンサユニット15が飽和するま
で繰り返す。
When one solid activated carbon electrode capacitor unit 15 is saturated, the switches 19a and 19b are sequentially switched so as to be connected to the other solid activated carbon electrode capacitor unit-switch contacts 20c and 20d. At this time, the solid activated carbon electrode capacitor unit 15 connected to the solid activated carbon electrode capacitor unit-switch contacts 20a and 20b released from the DC power supply 16 keeps adsorbing ions on the electric double layer. The same operation is repeated until all the solid activated carbon electrode capacitor units 15 are saturated.

【0030】このように、イオン吸着能を高めるために
複数の対の固体活性炭電極コンデンサユニットを設けた
場合において、これらのコンデンサユニットを一度に動
作させるのではなく、コンデンサユニット対を選択する
スイッチ盤19a、19bを順次回転して直流電源16
に接続することにより、直流電源16を大型化すること
なくイオン吸着能を高めることができる。
As described above, when a plurality of pairs of solid activated carbon electrode capacitor units are provided in order to enhance the ion adsorption capacity, a switch panel for selecting a capacitor unit pair is used instead of operating these capacitor units at once. 19a and 19b are sequentially rotated so that the DC power
, It is possible to increase the ion adsorption capacity without increasing the size of the DC power supply 16.

【0031】なお、本実施例では、固体活性炭電極の再
生については記載していないが、固体活性炭電極コンデ
ンサユニットの両外側又は隣り合うコンデンサユニット
対の間等に放出用電極を設け、濃縮用水を導入した後、
各コンデンサユニット対をショートさせ、放出用電極に
通電することにより、前記した第1の実施例と同様に固
体活性炭電極を再生することもできる。
In this embodiment, the regeneration of the solid activated carbon electrode is not described. However, a discharge electrode is provided on both outer sides of the solid activated carbon electrode capacitor unit or between adjacent capacitor unit pairs, and the concentrated water is supplied. After introduction,
By short-circuiting each capacitor unit pair and supplying current to the discharge electrode, the solid activated carbon electrode can be regenerated in the same manner as in the first embodiment.

【0032】また、イオンの吸着や固体活性炭電極の再
生に際して、被処理水や濃縮用水を攪拌し、反応効率を
高める構成としても良い。
Further, when adsorbing ions or regenerating a solid activated carbon electrode, the water to be treated and the water for concentration may be stirred to increase the reaction efficiency.

【0033】[0033]

【発明の効果】以上説明したように、本発明の活性炭電
極を用いたイオン性物質含有水の処理方法及び該活性炭
電極の再生方法並びにイオン性物質含有水の処理装置に
よれば、固体活性炭を両極に用いた処理装置によりイオ
ン性物質を電気二重層吸着し、活性炭吸着が飽和した際
には固体活性炭電極を含む回路をショートさせ、その後
固体活性炭電極の両外側等に配置したイオン吸着能を持
たない放出用電極に通電することにより、吸着したイオ
ンを高効率で放出させて固体活性炭を再生することがで
きる。
As described above, according to the method for treating ionic substance-containing water using the activated carbon electrode, the method for regenerating the activated carbon electrode, and the apparatus for treating ionic substance-containing water according to the present invention, solid activated carbon can be used. The treatment equipment used for both electrodes adsorbs ionic substances in the electric double layer, and when the activated carbon adsorption is saturated, shorts the circuit including the solid activated carbon electrode, and then reduces the ion adsorption capacity arranged on both sides of the solid activated carbon electrode. By energizing the discharge electrode that does not have the electrode, the adsorbed ions can be released with high efficiency to regenerate the solid activated carbon.

【0034】また、複数の固体活性炭電極が含まれてい
る場合に、それらを同時では無く分割して通電すること
により電源の小型化を維持しつつ、吸着能力を高めるこ
とができる。
Further, when a plurality of solid activated carbon electrodes are included, they are not divided at the same time, but are divided and energized, so that it is possible to maintain the miniaturization of the power supply and increase the adsorption capacity.

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

【図1】本発明の第1の実施例に係るイオン性物質含有
水の処理装置の構造を模式的に示す断面図である。
FIG. 1 is a cross-sectional view schematically showing a structure of an apparatus for treating ionic substance-containing water according to a first embodiment of the present invention.

【図2】本発明の第2の実施例に係るイオン性物質含有
水の処理装置の構造を模式的に示す断面図である。
FIG. 2 is a cross-sectional view schematically showing a structure of an apparatus for treating ionic substance-containing water according to a second embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 固体活性炭電極(陽極) 2 固体活性炭電極(陰極) 3 放出用電極(陽極) 4 放出用電極(陽極) 5 被処理水 6 処理用水槽 7 直流電源 8a〜8f 回路の状態を切り替えるためのスイッチ接
点 9 処理水 10 放流ライン 11 濃縮用水 12 濃縮用水移送ライン 13 濃縮用水槽 14 濃縮用水排出ライン 15 固体活性炭電極コンデンサユニット 16 直流電源 17a 電源−スイッチ接点(陽極用) 17b 電源−スイッチ接点(陰極用) 18a スイッチ盤(陽極用) 18b スイッチ盤(陰極用) 19a スイッチ(陽極用) 19b スイッチ(陽極用) 20a〜20d 固体活性炭電極コンデンサユニット−
スイッチ接点 21 処理水槽 22 被処理水
DESCRIPTION OF SYMBOLS 1 Solid activated carbon electrode (anode) 2 Solid activated carbon electrode (cathode) 3 Emission electrode (anode) 4 Emission electrode (anode) 5 Water to be treated 6 Treatment tank 7 DC power supply 8a to 8f Switch for switching circuit state Contact 9 Treated water 10 Release line 11 Concentration water 12 Concentration water transfer line 13 Concentration water tank 14 Concentration water discharge line 15 Solid activated carbon electrode capacitor unit 16 DC power supply 17a Power supply-switch contact (for anode) 17b Power supply-switch contact (for cathode) 18a Switch board (for anode) 18b Switch board (for cathode) 19a Switch (for anode) 19b Switch (for anode) 20a-20d Solid activated carbon electrode capacitor unit
Switch contact 21 Treated water tank 22 Treated water

───────────────────────────────────────────────────── フロントページの続き (72)発明者 齋藤 貴之 東京都港区芝五丁目7番1号 日本電気株 式会社内 (72)発明者 鱒沢 雅 神奈川県川崎市中原区下沼部1933番地10 日本電気環境エンジニアリング株式会社内 (72)発明者 菅沼 徹 神奈川県川崎市中原区下沼部1933番地10 日本電気環境エンジニアリング株式会社内 Fターム(参考) 4D024 AA01 AB15 BA02 BB05 BC01 DA04 DA07 DB09 4D061 DA01 DB13 EA10 EB04 EB14 EB19 EB29 EB37 FA06 GA06 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Takayuki Saito 5-7-1 Shiba, Minato-ku, Tokyo Within NEC Corporation (72) Inventor Masaru Masawa 1933-1033 Shimonumabe, Nakahara-ku, Kawasaki-shi, Kanagawa NEC Environmental Engineering Co., Ltd. (72) Inventor Toru Suganuma 1933-10 Shimonumabe, Nakahara-ku, Kawasaki-shi, Kanagawa F-term within NEC Environmental Engineering Co., Ltd. 4D024 AA01 AB15 BA02 BB05 BC01 DA04 DA07 DB09 4D061 DA01 DB13 EA10 EB04 EB14 EB19 EB29 EB37 FA06 GA06

Claims (10)

【特許請求の範囲】[Claims] 【請求項1】被処理水に含まれるイオン性物質を電気二
重層吸着して浄化する処理方法において、 処理槽内に、1以上の対をなす固体活性炭電極とイオン
吸着能を持たない一対の放出用電極とを備え、 前記被処理水を処理するに際し、直流電源を前記対をな
す固体活性炭電極に接続して前記イオン性物質を電気二
重層吸着し、 前記イオン性物質を吸着した前記固体活性炭電極を再生
するに際し、前記対をなす固体活性炭電極を短絡させた
後、前記直流電源を前記放出用電極に接続して前記固体
活性炭電極から前記イオン性物質を放出させることを特
徴とするイオン性物質含有水の処理方法。
1. A treatment method for purifying an ionic substance contained in water to be treated by electric double layer adsorption, wherein one or more pairs of a solid activated carbon electrode and a pair of non-ion-adsorbing electrodes are provided in a treatment tank. A discharge electrode, and when treating the water to be treated, a DC power supply is connected to the solid activated carbon electrode forming the pair to adsorb the ionic substance in the electric double layer, and the solid adsorbing the ionic substance is provided. When regenerating the activated carbon electrode, after short-circuiting the pair of solid activated carbon electrodes, the DC power supply is connected to the discharge electrode to release the ionic substance from the solid activated carbon electrode. Of water containing a toxic substance.
【請求項2】前記固体活性炭電極が活性炭/炭素複合材
料を含み、前記活性炭が活性炭粉末または活性炭繊維を
含み、前記炭素複合材料がフェノール樹脂の炭化物の複
合材料を含むことを特徴とする請求項1記載のイオン性
物質含有水の処理方法。
2. The solid activated carbon electrode comprises an activated carbon / carbon composite material, the activated carbon comprises activated carbon powder or activated carbon fiber, and the carbon composite material comprises a phenolic carbide composite material. The method for treating ionic substance-containing water according to claim 1.
【請求項3】前記固体活性炭電極の再生に際し、前記イ
オン性物質が吸着された前記被処理水を放流し、予め設
けた再生用の水槽から前記処理槽に再生用水を注入して
前記固体活性炭電極の再生を行い、再生が終了したら再
び前記再生用水を前記再生用水槽に移送することを特徴
とする請求項1又は2に記載のイオン性物質含有水の処
理方法。
3. When the solid activated carbon electrode is regenerated, the water to be treated to which the ionic substance is adsorbed is discharged, and water for regeneration is injected into the treatment tank from a water tank for regeneration provided in advance. The method for treating ionic substance-containing water according to claim 1, wherein the regeneration of the electrode is performed, and after the regeneration is completed, the regeneration water is transferred to the regeneration water tank again.
【請求項4】前記一対の放出用電極を前記対をなす固体
活性炭電極の両外側に配設し、かつ、電極の極性を前記
放出用電極と前記固体活性炭電極とで逆となるように設
定することを特徴とする請求項1又乃至3のいずれか一
に記載のイオン性物質含有水の処理方法。
4. The pair of discharge electrodes are disposed on both outer sides of the pair of solid activated carbon electrodes, and the polarities of the electrodes are set to be opposite between the discharge electrode and the solid activated carbon electrode. The method for treating ionic substance-containing water according to any one of claims 1 to 3, wherein the ionic substance-containing water is treated.
【請求項5】前記固体活性炭電極の対を複数備え、各々
の対を順次選択して前記直流電源に接続して吸着処理を
行うことを特徴とする請求項1又乃至4のいずれか一に
記載のイオン性物質含有水の処理方法。
5. The method according to claim 1, wherein a plurality of pairs of the solid activated carbon electrodes are provided, and each of the pairs is sequentially selected and connected to the DC power supply to perform an adsorption process. A method for treating ionic substance-containing water according to the above.
【請求項6】被処理水中のイオン性物質を電気二重層吸
着して浄化する処理装置において、 処理槽と、1以上の対をなす固体活性炭電極と、イオン
吸着能を持たない一対の放出用電極と、直流電源と、該
直流電源と接続される電極を選択する切り替え手段と、
前記対をなす固体活性炭電極を相互に短絡させる回路と
を少なくとも有し、 前記被処理水を処理するに際し、前記直流電源と前記対
をなす固体活性炭電極とが接続されて前記イオン性物質
が電気二重層吸着され、 前記イオン性物質を吸着した前記固体活性炭電極を再生
するに際し、前記短絡回路によって前記対をなす固体活
性炭電極が短絡され、前記切り替え手段によって前記直
流電源と前記放出用電極とが接続されて前記固体活性炭
電極から前記イオン性物質が放出されることを特徴とす
るイオン性物質含有水の処理装置。
6. A treatment apparatus for purifying ionic substances in water to be treated by electric double layer adsorption, comprising: a treatment tank, one or more pairs of solid activated carbon electrodes, and a pair of dischargers having no ion adsorption ability. An electrode, a DC power supply, and switching means for selecting an electrode connected to the DC power supply;
At least a circuit for short-circuiting the pair of solid activated carbon electrodes with each other, and when treating the water to be treated, the DC power supply and the solid activated carbon electrode forming the pair are connected, and the ionic substance is electrically charged. Upon regeneration of the solid activated carbon electrode adsorbed with the double layer and adsorbing the ionic substance, the short-circuit circuit short-circuits the paired solid activated carbon electrodes, and the switching means causes the DC power supply and the discharge electrode to be short-circuited. The apparatus for treating ionic substance-containing water, wherein the ionic substance is discharged from the solid activated carbon electrode when connected.
【請求項7】前記固体活性炭電極が活性炭/炭素複合材
料を含み、前記活性炭が活性炭粉末または活性炭繊維を
含み、前記炭素複合材料がフェノール樹脂の炭化物の複
合材料を含むことを特徴とする請求項6記載のイオン性
物質含有水の処理装置。
7. The solid activated carbon electrode includes an activated carbon / carbon composite material, the activated carbon includes activated carbon powder or activated carbon fiber, and the carbon composite material includes a phenolic carbide composite material. 7. An apparatus for treating ionic substance-containing water according to 6.
【請求項8】前記処理槽に、処理済みの前記被処理水を
放出する放出経路と、前記固体活性炭電極の再生に用い
る再生用水を蓄える再生用水槽と接続する再生用水移送
経路とが設けられ、前記固体活性炭電極の再生に際し、
前記イオン性物質が吸着された前記被処理水が前記放出
経路から放流され、前記再生用水槽から前記処理槽に再
生用水が注入されて前記固体活性炭電極の再生が行わ
れ、再生が終了したら前記再生用水が再び前記再生用水
槽に移送されることを特徴とする請求項6又は7に記載
のイオン性物質含有水の処理装置。
8. The treatment tank is provided with a discharge path for releasing the treated water to be treated and a regeneration water transfer path connected to a regeneration water tank for storing regeneration water used for regeneration of the solid activated carbon electrode. Upon regeneration of the solid activated carbon electrode,
The water to be treated, to which the ionic substance is adsorbed, is discharged from the release path, regeneration water is injected from the regeneration water tank into the treatment tank, and the solid activated carbon electrode is regenerated. The apparatus for treating ionic substance-containing water according to claim 6 or 7, wherein the regeneration water is transferred to the regeneration water tank again.
【請求項9】前記一対の放出用電極が前記対をなす固体
活性炭電極の両外側に配設され、かつ、電極の極性が前
記放出用電極と前記固体活性炭電極とで逆となるように
設定されることを特徴とする請求項6又乃至8のいずれ
か一に記載のイオン性物質含有水の処理装置。
9. The pair of discharge electrodes are arranged on both outer sides of the pair of solid activated carbon electrodes, and the polarity of the electrodes is set to be opposite between the discharge electrodes and the solid activated carbon electrodes. The ionic substance-containing water treatment apparatus according to claim 6, wherein the ionic substance-containing water is treated.
【請求項10】前記固体活性炭電極の対を複数備え、前
記切り替え手段によって前記対をなす固体活性炭電極が
順次選択させてイオンの吸着が行われることを特徴とす
る請求項6乃至9のいずれか一に記載のイオン性物質含
有水の処理装置。
10. The method according to claim 6, wherein a plurality of said pairs of solid activated carbon electrodes are provided, and said switching means selects said pair of solid activated carbon electrodes sequentially to perform ion adsorption. An apparatus for treating ionic substance-containing water according to claim 1.
JP2001079075A 2001-03-19 2001-03-19 Treating device and treating method for ionic substance- containing water using activated carbon electrode and regenerating method of activated carbon electrode Withdrawn JP2002273434A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006247640A (en) * 2005-02-08 2006-09-21 Air Water Inc Apparatus for adjusting concentration of electrified substance in liquid, and apparatus and method for controlling quality of solution
GB2475168A (en) * 2009-11-05 2011-05-11 Arvia Technology Ltd Method for the treatment of liquids using regeneratable adsorbent material
CN102690004A (en) * 2012-06-12 2012-09-26 爱思特水务科技有限公司 Electro-adsorption module modification system and process
JP2014127466A (en) * 2012-12-26 2014-07-07 Kazuhiro Hayashi Promoting step of material movement between electrodes in electrolyte by applying voltage
CN104828909A (en) * 2015-05-16 2015-08-12 赵东旭 Wastewater treatment device

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006247640A (en) * 2005-02-08 2006-09-21 Air Water Inc Apparatus for adjusting concentration of electrified substance in liquid, and apparatus and method for controlling quality of solution
GB2475168A (en) * 2009-11-05 2011-05-11 Arvia Technology Ltd Method for the treatment of liquids using regeneratable adsorbent material
GB2475168B (en) * 2009-11-05 2013-01-09 Arvia Technology Ltd Method for the treatment of liquids using regeneratable adsorbent material
CN102690004A (en) * 2012-06-12 2012-09-26 爱思特水务科技有限公司 Electro-adsorption module modification system and process
JP2014127466A (en) * 2012-12-26 2014-07-07 Kazuhiro Hayashi Promoting step of material movement between electrodes in electrolyte by applying voltage
CN104828909A (en) * 2015-05-16 2015-08-12 赵东旭 Wastewater treatment device

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