JP2003290773A - Ionization cleaning device - Google Patents

Ionization cleaning device

Info

Publication number
JP2003290773A
JP2003290773A JP2002098177A JP2002098177A JP2003290773A JP 2003290773 A JP2003290773 A JP 2003290773A JP 2002098177 A JP2002098177 A JP 2002098177A JP 2002098177 A JP2002098177 A JP 2002098177A JP 2003290773 A JP2003290773 A JP 2003290773A
Authority
JP
Japan
Prior art keywords
ionization
electrodes
electrode
auxiliary electrode
wastewater
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.)
Granted
Application number
JP2002098177A
Other languages
Japanese (ja)
Other versions
JP3692327B2 (en
Inventor
Sotohiro Maruyama
外弘 丸山
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP2002098177A priority Critical patent/JP3692327B2/en
Publication of JP2003290773A publication Critical patent/JP2003290773A/en
Application granted granted Critical
Publication of JP3692327B2 publication Critical patent/JP3692327B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

<P>PROBLEM TO BE SOLVED: To prolong the service life of an electrode by removing contaminants from waste water while removing scale adhering to the electrode, and to provide an ionization cleaning device in which the removal effect of the contaminants is improved even when voltage applied between the electrodes is decreased. <P>SOLUTION: In the ionization cleaning device which removes the contaminants in the waste water by applying direct current voltage to the electrodes arranged in a septic tank containing the waste water, the electrodes are disposed movably and the scale adhering to the surfaces of the electrodes is removed by moving the electrodes while rotating the electrodes. <P>COPYRIGHT: (C)2004,JPO

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、工業廃水や生活廃
水を電離イオン化によって浄化する電離イオン化浄化装
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 ionization / ionization purification apparatus for purifying industrial wastewater and domestic wastewater by ionization ionization.

【0002】[0002]

【従来の技術】産業廃水や生活廃水、家畜等の糞尿が混
合した廃水(以下、総称して「廃水」という)は、直接河
川や下水等に放出したり再利用できないため、一旦浄化
を行なう必要がある。廃水に含まれる汚濁物質には、コ
ロイド状の微細粒子や、リン成分、COD、SS等があ
る。これら汚濁物質は、一般に正又は負に帯電してお
り、同種の電荷を帯びた粒子どうしが反発しあうため凝
集し難く、回収が困難である。
2. Description of the Related Art Industrial wastewater, domestic wastewater, and wastewater mixed with human excrement (hereinafter collectively referred to as "wastewater") cannot be directly discharged to rivers or sewage or reused, so it is once purified. There is a need. The pollutants contained in the wastewater include colloidal fine particles, phosphorus components, COD, SS and the like. These pollutants are generally positively or negatively charged, and particles having the same type of charge repel each other, so that they are difficult to aggregate and difficult to collect.

【0003】電荷を帯びた汚濁物質の処理方法として、
電離イオン化法が知られている。電離イオン化法は、図
5に示すように、浄化槽(90)中に一対の電極(92)(94)を
配置し、両電極(92)(94)間に直流電圧を印加して、廃水
中の汚濁物質の電荷を中和、消失又は低下させて、汚濁
物質を相互に凝集させるものである。凝集した汚濁物質
(フロック)にはバブリングによる微細気泡を当てること
によって、フロックに微細気泡が吸着し、フロックを浮
上分離できる。電極として、アルミニウムやアルミニウ
ム合金等から構成される電極と、ステンレス、酸化鉄等
から構成される電極が用いられ、これら電極間に直流電
圧を印加すると、アルミニウム電極からアルミニウムイ
オンが電離し、この電離したアルミニウムイオンの凝集
作用により廃水中の汚濁物質が凝集してフロックとな
る。
As a method for treating charged pollutants,
The ionization ionization method is known. In the ionization ionization method, as shown in FIG. 5, a pair of electrodes (92) and (94) are arranged in a septic tank (90), and a DC voltage is applied between both electrodes (92) and (94) to remove wastewater. It neutralizes, eliminates or reduces the electric charge of the pollutant, and causes the pollutant to aggregate with each other. Aggregated pollutants
By bubbling fine air bubbles to the (flock), the fine air bubbles are adsorbed on the flock and the flocs can be floated and separated. As electrodes, electrodes made of aluminum, aluminum alloys, etc. and electrodes made of stainless steel, iron oxide, etc. are used. When a DC voltage is applied between these electrodes, aluminum ions are ionized from the aluminum electrodes. Due to the aggregating action of the aluminum ions, the pollutants in the wastewater agglomerate into flocs.

【0004】電離イオン化法は、特に廃水中のリン、ノ
ルマルヘキサン、COD、脱色等の成分を除去するのに
有効な方法である。
The ionization ionization method is an effective method for removing components such as phosphorus, normal hexane, COD and decolorization in wastewater.

【0005】[0005]

【発明が解決しようとする課題】上記電離イオン化法
は、電極成分のイオン電離によって反応が進行するた
め、長期の使用により電極が薄くなったり、汚濁物質が
スケールとして電極表面に付着し、電極間に流れる電圧
が低下する問題があり、通常、1〜3ヶ月毎に電極を交
換する必要があった。また、汚濁物質の除去効率を高め
るには、電極間に約6〜40V、約30〜100Aの電
流を流す必要がある。
In the above-mentioned ionization ionization method, since the reaction proceeds due to ionization of the electrode components, the electrode becomes thin due to long-term use, or contaminants adhere to the surface of the electrode as a scale, and There is a problem that the voltage flowing through the electrodes decreases, and it is usually necessary to replace the electrodes every 1 to 3 months. Further, in order to increase the efficiency of removing contaminants, it is necessary to pass a current of about 6 to 40 V and about 30 to 100 A between the electrodes.

【0006】本発明の目的は、電極に付着するスケール
を除去しつつ、廃水からの汚濁物質の除去を図ることに
より、電極の長寿命化を図り、且つ、汚濁物質の除去効
果を高めることのできる電離イオン化浄化装置を提供す
ることである。
An object of the present invention is to remove the scale adhering to the electrode and to remove the pollutant from the wastewater, thereby extending the life of the electrode and enhancing the effect of removing the pollutant. It is an object of the present invention to provide an ionization / ionization purification device capable of performing ionization.

【0007】[0007]

【課題を解決するための手段】上記課題を解決するため
に、本発明の電離イオン化浄化装置は、廃水を含む浄化
槽中に配置された電極に直流電圧を印加することによっ
て、廃水中の汚濁物質を除去する電離イオン化浄化装置
において、電極を移動可能に配備し、電極を回転させつ
つ移動させることによって該電極の表面に付着したスケ
ールを除去できるようにしたものである。
In order to solve the above-mentioned problems, the ionization / ionization purifying apparatus of the present invention applies a DC voltage to electrodes arranged in a septic tank containing waste water to thereby pollute substances in the waste water. In the ionization / ionization purifying apparatus for removing the above, the electrode is movably provided, and the scale attached to the surface of the electrode can be removed by moving the electrode while rotating the electrode.

【0008】[0008]

【作用及び効果】浄化槽中に配置された電極は、回転移
動可能であるから、電極の回転によって、電極の極性が
変化し、表面に付着したスケールが除去される。また、
回転移動の際に、電極どうしが擦り合わされることによ
り、表面に付着したスケールが除去される。さらに、電
極を廃水中から露出させて露出部分を洗浄する場合に
は、露出部分の電極表面に付着したスケールが洗浄によ
り除去される。汚濁物質の除去作業中に、電極表面に付
着したスケールも除去されるから、電極表面の導電性が
低下することなく、長期に亘って高い電極反応を維持す
ることができ、廃水中の汚濁物質を効果的に除去でき
る。
[Operation and effect] Since the electrode placed in the septic tank is rotatable, the rotation of the electrode changes the polarity of the electrode and removes the scale adhering to the surface. Also,
During the rotational movement, the electrodes are rubbed against each other, so that the scale attached to the surface is removed. Further, when the electrode is exposed from the waste water and the exposed portion is washed, the scale attached to the electrode surface of the exposed portion is removed by washing. During the work of removing contaminants, the scale adhering to the electrode surface is also removed, so it is possible to maintain a high electrode reaction for a long period of time without lowering the conductivity of the electrode surface, and contaminants in wastewater Can be effectively removed.

【0009】[0009]

【発明の実施の形態】<実施形態1>図1は、本発明の
電離イオン化浄化装置(10)の一実施例を示す斜視図であ
る。電離イオン化浄化装置(10)は、廃水が投入される浄
化槽(12)の内部に一対の主電極(20)(22)を配置し、該主
電極(20)(22)間に複数の補助電極(30)(30)を配置して構
成される。補助電極(30)は、後述のとおり、補助電極移
動手段(32)に収容される。
BEST MODE FOR CARRYING OUT THE INVENTION <First Embodiment> FIG. 1 is a perspective view showing an embodiment of an ionization / ionization purification device (10) of the present invention. The ionization / ionization purification device (10) has a pair of main electrodes (20) and (22) arranged inside a septic tank (12) into which wastewater is charged, and a plurality of auxiliary electrodes between the main electrodes (20) and (22). (30) It is configured by arranging (30). The auxiliary electrode (30) is housed in the auxiliary electrode moving means (32) as described later.

【0010】浄化槽(12)は、FRP(繊維強化プラスチ
ック)等の材料から作製される筐体であって、廃水を浄
化槽(12)に流入させる流入管(14)と、浄化後の廃水が排
出される排水管(16)が形成されている。流入管(14)は、
浄化槽(12)の下部近傍で開口することが望ましく、排水
管(16)は、浄化槽(12)の上部近傍で開口することが望ま
しい。
The septic tank (12) is a casing made of a material such as FRP (fiber reinforced plastic), and has an inflow pipe (14) for letting the wastewater into the septic tank (12) and the wastewater after purification is discharged. A drainage pipe (16) is formed. The inflow pipe (14) is
It is desirable to open near the lower part of the septic tank (12), and it is desirable that the drain pipe (16) open near the upper part of the septic tank (12).

【0011】主電極(20)(22)は、直流電圧を供給する電
源装置(18)に電気的に接続され、廃液中に一部又は全部
が浸漬するよう配置されている。主電極(20)(22)の大き
さ、形状は、特に限定されるものではないが、後述する
補助電極移動手段(32)のケース(34)の端面と同程度の大
きさとすることが望ましい。主電極(20)(22)の材質は、
FeやAl又はこれらの合金、さらには強度を高めるた
めにセラミック等を含有した材料から作製できる。
The main electrodes (20) and (22) are electrically connected to a power supply device (18) which supplies a DC voltage, and are arranged so as to be partially or wholly immersed in the waste liquid. The size and shape of the main electrodes (20) and (22) are not particularly limited, but it is desirable that the size and shape are approximately the same as the end surface of the case (34) of the auxiliary electrode moving means (32) described later. . The material of the main electrodes (20) (22) is
It can be made of Fe, Al, or an alloy thereof, or a material containing ceramic or the like for increasing strength.

【0012】主電極(20)(22)間に配備される補助電極(3
0)(30)は、Al−Fe合金等の材料から作製できる。補
助電極(30)の形状は、球状が望ましいが、球状以外の形
状、例えば、楕円状、円柱状、角柱状のものや、金属塊
を破砕したものなどでもよい。補助電極(30)(30)の表面
には、水酸化被膜等の被膜を形成しておくことが望まし
い。水酸化被膜は、Al、Mg及びCaを主成分とし、
その他Fe、Ni、Cr等を少量含む構成とすることが
できる。補助電極(30)の外径は、3〜10cm程度、望
ましくは5cm前後が適当であり、同一外径のものだけ
でもよいが、外径の異なるものを混ぜて用いると、補助
電極(30)どうしの接触効率が高まり、スケール除去効果
を高めることができる。また、収容される補助電極(30)
の個数は、補助電極(30)を収容するケース(34)(後述す
る)の大きさに応じて異なるが、ケース(34)の内部で補
助電極(30)が自由に移動でき得る程度の量を収容するこ
とが望ましい。
An auxiliary electrode (3) provided between the main electrodes (20) and (22)
(0) (30) can be made from a material such as an Al-Fe alloy. The auxiliary electrode (30) preferably has a spherical shape, but may have a shape other than the spherical shape, for example, an elliptical shape, a cylindrical shape, a prismatic shape, or a crushed metal mass. It is desirable to form a coating such as a hydroxide coating on the surfaces of the auxiliary electrodes (30) (30). The hydroxide film is mainly composed of Al, Mg and Ca,
In addition, a small amount of Fe, Ni, Cr or the like may be included. The outer diameter of the auxiliary electrode (30) is about 3 to 10 cm, preferably about 5 cm, and the outer diameter may be the same. However, if the electrodes having different outer diameters are mixed and used, the auxiliary electrode (30) The contact efficiency between them is enhanced, and the scale removal effect can be enhanced. Also, the auxiliary electrode (30) to be housed
The number of the auxiliary electrodes (30) varies depending on the size of the case (34) (described later) that accommodates the auxiliary electrode (30), but is an amount that allows the auxiliary electrode (30) to move freely inside the case (34). It is desirable to accommodate

【0013】上記補助電極(30)(30)は、主電極(20)(22)
間に配備された補助電極ケース(34)に収容される。該ケ
ース(34)は、主電極(20)(22)に端面が接近して配置され
た筒状体であり、軸心に回転軸(36)が取り付けられ、該
回転軸(36)が、モータ等を駆動源とする回転駆動手段(3
8)に連繋されている。ケース(34)の両端面と主電極(20)
(22)との間隔は、接近させるほど好ましく、数mm〜数
cm程度とすることが望ましい。ケース(34)は、Al−
Fe合金から作製することができる。ケース(34)の周壁
又は側壁に、廃水をケース(34)の内部に流入させるため
の孔(35)(35)が複数開設されている。
The auxiliary electrodes (30) (30) are the main electrodes (20) (22).
It is housed in the auxiliary electrode case (34) provided between them. The case (34) is a cylindrical body whose end faces are arranged close to the main electrodes (20) (22), and the rotating shaft (36) is attached to the shaft center, and the rotating shaft (36) is Rotational drive means (3
It is linked to 8). Both ends of case (34) and main electrode (20)
The closer to (22), the closer it is, and preferably about several mm to several cm. The case (34) is made of Al-
It can be made from a Fe alloy. A plurality of holes (35) (35) for allowing wastewater to flow into the case (34) are formed in the peripheral wall or the side wall of the case (34).

【0014】補助電極(30)(30)に付着するスケールを効
率よく除去し、凝集したフロックを浮上させ、また、浄
化槽(12)の内部の廃水を循環させるために、ケース(34)
の内部にバブリング手段(13)を配備することが望まし
い。なお、補助電極(30)(30)のスケール除去には、補助
電極(30)(30)に超音波を照射することも効果的である。
また、ケース(34)内の補助電極(30)の移動を促進するた
めに、ケース(34)内に1又は複数の突起又は突条(図示
せず)を設けてもよい。
The case (34) is used to efficiently remove the scale attached to the auxiliary electrodes (30) (30), float flocculated flocs, and circulate the waste water inside the septic tank (12).
It is desirable to arrange bubbling means (13) inside. For removing the scale of the auxiliary electrodes (30) (30), it is effective to irradiate the auxiliary electrodes (30) (30) with ultrasonic waves.
Further, in order to promote the movement of the auxiliary electrode (30) in the case (34), one or more protrusions or ridges (not shown) may be provided in the case (34).

【0015】上記構成の電離イオン化浄化装置(10)によ
る廃水浄化工程について説明する。まず、流入管(14)か
ら浄化槽(12)に廃水を導入する。主電極(20)(22)及びケ
ース(34)がほぼ廃水に浸漬した状態で、主電極(20)(22)
間に電源装置(18)から直流電圧を印加するとともに、回
転駆動手段(38)を駆動して、ケース(34)を回転させる。
主電極(20)(22)間には、4〜30Vの電圧を印加する。
なお、これよりも高電圧で作動させることも勿論可能で
ある。主電極(20)(20)間に流れる電流値は、補助電極(3
0)(30)の存在により、従来よりも低く抑えることができ
る。
A waste water purification process by the ionization / ionization purification device (10) having the above structure will be described. First, waste water is introduced into the septic tank (12) from the inflow pipe (14). With the main electrodes (20) (22) and case (34) almost immersed in wastewater, the main electrodes (20) (22)
A DC voltage is applied from the power supply device (18) in the meantime, and the rotation drive means (38) is driven to rotate the case (34).
A voltage of 4 to 30 V is applied between the main electrodes (20) and (22).
It is of course possible to operate at a voltage higher than this. The current value flowing between the main electrodes (20) (20) is
Due to the existence of 0) and (30), it can be suppressed to a lower level than before.

【0016】主電極(20)(22)間に直流電圧を印加するこ
とにより、負に荷電している主電極(20)から金属イオン
(例えばアルミニウムイオン)が溶出し、廃水中の汚濁物
質(コロイド状の粒子であって、一般に負に荷電してい
る)の電位を中和、低下又は消失させる。この電極反応
により、汚濁物質が相互に凝集してフロックとなる。主
電極(20)(22)間に配備された補助電極(30)(30)は、主電
極(20)(22)間に直流電圧を印加すると残余電流が発生
し、補助電極(30)(30)は、マイナス側の主電極(20)に近
い側が正に荷電し、プラス側主電極(22)に近い側が負に
荷電する。その結果、各補助電極(30)においても、電極
反応が生じ、汚濁物質の電位が中和、低下又は消失し、
汚濁物質が相互に凝集する。上述のように、主電極(20)
(22)だけでなく補助電極(30)(30)による電極反応によ
り、廃水中の汚濁物質が凝集してフロックとなり、バブ
リング手段(13)によってフロックに微細気泡を吸着させ
ることにより、汚濁物質を浮上分離させることができ
る。
By applying a DC voltage between the main electrodes (20) and (22), metal ions are charged from the negatively charged main electrode (20).
(For example, aluminum ions) elute and neutralize, reduce or eliminate the potential of pollutants (colloidal particles, which are generally negatively charged) in wastewater. By this electrode reaction, contaminants aggregate with each other to form flocs. The auxiliary electrodes (30) and (30) arranged between the main electrodes (20) and (22) generate residual electric current when a DC voltage is applied between the main electrodes (20) and (22), and the auxiliary electrodes (30) ( As for 30), the side close to the negative side main electrode (20) is positively charged, and the side close to the plus side main electrode (22) is negatively charged. As a result, also in each auxiliary electrode (30), an electrode reaction occurs, the potential of the pollutant is neutralized, reduced or disappears,
Pollutants aggregate with each other. As mentioned above, the main electrode (20)
(22) In addition to the electrode reaction by the auxiliary electrodes (30) and (30), the pollutants in the wastewater are aggregated into flocs, and the bubbling means (13) adsorbs the pollutants by adsorbing fine bubbles to the flocs. Can be floated and separated.

【0017】補助電極(30)(30)での電極反応が進むにつ
れて、補助電極(30)(30)の表面にスケールが付着する。
スケールが補助電極(30)(30)の表面に付着すると、電極
反応が低下し、浄化能力が大きく低下する。しかしなが
ら、本発明では、補助電極(30)(30)をケース(34)に収容
し、該ケース(34)を回転させている。その結果、内部に
収容された補助電極(30)(30)は、ケース(34)内で回転す
る。補助電極(30)の転動により、各補助電極(30)は、電
気的な極性が変わるから、その極性変化により付着した
スケールが除去される。また、回転に伴い、補助電極(3
0)(30)は互いに又はケース(34)の内面に衝突しながら移
動する。その結果、補助電極(30)(30)の表面に付着した
スケールが剥離し、バブリングによる微細気泡に吸着さ
れて、汚濁物質と共に浮上して分離される。つまり、補
助電極(30)(30)へのスケールの付着を避けることができ
るから、長期に亘って高効率の電極反応を行なうことが
でき、また、補助電極(30)(30)の交換、清掃等の間隔も
長くすることができる。なお、補助電極ケース(34)の回
転は、補助電極(30)(30)のスケール付着具合や、廃水の
汚濁程度に合わせて、連続的に行なってもよいし、間欠
的に行なってもよい。
As the electrode reaction at the auxiliary electrodes (30) (30) progresses, scale adheres to the surfaces of the auxiliary electrodes (30) (30).
When the scale adheres to the surface of the auxiliary electrodes (30) (30), the electrode reaction is reduced and the purification ability is greatly reduced. However, in the present invention, the auxiliary electrodes (30) (30) are housed in the case (34) and the case (34) is rotated. As a result, the auxiliary electrodes (30) (30) housed inside rotate in the case (34). Since the electric polarity of each auxiliary electrode (30) changes due to the rolling of the auxiliary electrode (30), the attached scale is removed by the change in the polarity. In addition, the auxiliary electrode (3
0) and (30) move while colliding with each other or the inner surface of the case (34). As a result, the scale attached to the surfaces of the auxiliary electrodes (30) (30) is peeled off, adsorbed by the fine bubbles due to bubbling, and floated up and separated together with the contaminants. That is, since it is possible to avoid the adhesion of scale to the auxiliary electrodes (30) (30), it is possible to perform a highly efficient electrode reaction for a long period of time, and also to replace the auxiliary electrodes (30) (30), The interval for cleaning and the like can be lengthened. The rotation of the auxiliary electrode case (34) may be performed continuously or intermittently depending on the scale adhesion of the auxiliary electrodes (30) and (30) and the degree of pollution of waste water. .

【0018】上記構成の電離イオン化浄化装置(10)は、
例えば、図2に示すような浄化システム(60)に組み込ん
で用いることができる。浄化システム(60)は、循環槽(6
2)と、該循環槽(62)に接続された本発明の電離イオン化
浄化装置(10)と、循環槽(62)の下流側に配備された高分
子反応槽(68)と、該高分子反応槽(68)の下流側に配備さ
れた浮上槽(69)とを具えた構成とすることができる。
The ionization / purification device (10) having the above structure is
For example, it can be used by incorporating it into a purification system (60) as shown in FIG. The purification system (60) has a circulation tank (6
2), the ionization / ionization purification device (10) of the present invention connected to the circulation tank (62), a polymer reaction tank (68) arranged downstream of the circulation tank (62), and the polymer It may be configured to include a floating tank (69) arranged on the downstream side of the reaction tank (68).

【0019】循環槽(62)は、ステンレス鋼等から作製さ
れる筐体であって、廃水が導入される廃水導入管(63)
と、浄化装置(10)の流入管(14)に接続され、廃水の一部
を電離イオン化浄化装置(10)に導く配管(64)と、浄化さ
れた廃水を高分子反応槽(68)に導出する排水管(65)を具
える。循環槽(62)には、浄化効率を高めるために、直流
電源に接続された一対又は複数対の電極を配備してもよ
い。また、循環槽(62)の底部に、汚濁物質を浮上分離さ
せるためのバブリング手段(67)を配置してもよい。さら
に、循環槽(62)に、ポリ塩化アルミニウムや、硫酸バン
ド、塩化第1鉄、塩化第2鉄等の薬品を投入し、廃水中
の汚濁物質を中和して凝集させて回収し、浄化効率を高
めてもよい。
The circulation tank (62) is a casing made of stainless steel or the like, and a wastewater introduction pipe (63) into which wastewater is introduced.
And a pipe (64) connected to the inflow pipe (14) of the purification device (10) and guiding a part of the waste water to the ionization and ionization purification device (10), and the purified waste water to the polymer reaction tank (68). It is equipped with a drainage pipe (65). The circulation tank (62) may be provided with a pair of electrodes or a plurality of pairs of electrodes connected to a DC power source in order to enhance the purification efficiency. Further, bubbling means (67) for floating and separating pollutants may be arranged at the bottom of the circulation tank (62). Furthermore, chemicals such as polyaluminum chloride, sulfuric acid band, ferrous chloride and ferric chloride are put in the circulation tank (62) to neutralize and collect pollutants in the wastewater to collect and purify them. You may increase efficiency.

【0020】循環槽(62)に導入された廃水の一部は、配
管(64)を通って、電離イオン化浄化装置(10)に流入す
る。配管(64)には、経路中にポンプ手段(66)が挿入され
ており、ポンプ手段(66)の駆動によって、循環槽(62)か
ら浄化装置(10)に廃水が送給される。
A part of the waste water introduced into the circulation tank (62) flows into the ionization / ionization purification device (10) through the pipe (64). A pump means (66) is inserted in the path of the pipe (64), and the waste water is fed from the circulation tank (62) to the purification device (10) by driving the pump means (66).

【0021】浄化装置(10)に流入した廃水は、上記のと
おり、主電極(20)(22)及び補助電極(30)(30)による電極
反応により浄化され、排水管(16)から循環槽(62)に戻さ
れる。
The wastewater that has flowed into the purification device (10) is purified by the electrode reaction of the main electrodes (20) (22) and the auxiliary electrodes (30) (30) as described above, and is discharged from the drain pipe (16) to the circulation tank. Returned to (62).

【0022】循環槽(62)及び浄化装置(10)で浄化された
廃水は、循環槽(62)の下流側に設けられた高分子反応槽
(68)に送られる。高分子反応槽(68)では、高分子凝集剤
(例えばアニリン系等)を投入し、薬剤処理を行なう。必
要に応じて、高分子反応槽(68)には、内部の廃水を撹拌
する手段を設けてもよい。
The wastewater purified by the circulation tank (62) and the purification device (10) is a polymer reaction tank provided on the downstream side of the circulation tank (62).
Sent to (68). In the polymer reaction tank (68), the polymer flocculant
(For example, an aniline type) is charged and a chemical treatment is performed. If necessary, the polymer reaction tank (68) may be provided with a means for stirring the waste water inside.

【0023】高分子反応槽(68)における薬剤処理により
汚濁物質が除去された廃水は、反応槽(68)の下流側に設
けられた浮上槽(69)に送られる。浮上槽(69)では、フロ
ックにバブリングを施し、フロックを浮上分離させて回
収する。回収された浮上物は、廃棄又は植物の肥料等と
して利用できる。
The wastewater from which pollutants have been removed by the chemical treatment in the polymer reaction tank (68) is sent to the flotation tank (69) provided on the downstream side of the reaction tank (68). In the flotation tank (69), bubbling is performed on the flocs, and the flocs are levitated and collected. The collected floating material can be discarded or used as plant fertilizer or the like.

【0024】上記浄化システム(60)で廃水を浄化するこ
とにより、廃水中に含まれるリン成分、窒素成分、有機
成分、無機成分等の汚濁物質をほとんど除去できる。
By purifying the wastewater with the purification system (60), most of the pollutants such as phosphorus, nitrogen, organic and inorganic components contained in the wastewater can be removed.

【0025】異なる実施形態として、図3に示すよう
に、補助電極ケース(34)を円筒状に形成し、該円筒状の
ケース(34)の内面下部に、補助電極(30)(30)を撹拌によ
り移動させる撹拌部材(40)を具えたものを例示できる。
撹拌部材(40)として、羽根状のものを例示できる。ケー
ス(34)の底部に非導電性部材(42)を介在させて主電極(2
0)を配備し、ケース(34)の上部には主電極(22)が配備さ
れる。非導電性部材(42)を配備したのは、補助電極(30)
と主電極(20)が直接接触しないようにするためである。
撹拌部材(40)は、中心位置が回転軸(44)に接続され、モ
ータ(46)によって回転可能となっている。ケース(34)の
周面及び/又は底面には廃水が流通可能な孔が複数開設
されており、ケース(34)内に廃水を導入した状態で、撹
拌部材(40)を回転させると、主電極(20)(22)間に配備さ
れた補助電極(30)(30)が、撹拌部材(40)によってケース
(34)内で回転しながら移動する。これにより、廃水の電
離イオン分解が行なわれると共に、補助電極(30)(30)の
転動による電気的な極性変化と、補助電極(30)(30)どう
しの擦り合わせにより、補助電極(30)(30)の表面に付着
したスケールの除去を行なうことができる。なお、主電
極(20)(22)は、円筒状又は半円筒状に形成して、ケース
(34)の内面又は外周面に配備してもよい。
As a different embodiment, as shown in FIG. 3, the auxiliary electrode case (34) is formed into a cylindrical shape, and the auxiliary electrodes (30) and (30) are provided on the lower portion of the inner surface of the cylindrical case (34). An example is one including a stirring member (40) that is moved by stirring.
An example of the stirring member (40) is a blade. A non-conductive member (42) is interposed at the bottom of the case (34) to connect the main electrode (2
0) is provided, and the main electrode (22) is provided on the upper part of the case (34). The non-conductive member (42) is arranged in the auxiliary electrode (30).
This is to prevent the main electrode (20) from directly contacting with.
The stirring member (40) is connected to the rotating shaft (44) at the center position and can be rotated by the motor (46). A plurality of holes through which waste water can flow are provided on the peripheral surface and / or the bottom surface of the case (34), and when the stirring member (40) is rotated with the waste water introduced into the case (34), the main Auxiliary electrodes (30) (30) arranged between the electrodes (20) (22) are cased by the stirring member (40).
Move while rotating in (34). As a result, the ionization ion decomposition of the waste water is performed, and the auxiliary electrode (30) is rubbed with each other due to the electrical polarity change caused by the rolling of the auxiliary electrodes (30) and (30). ) It is possible to remove the scale attached to the surface of (30). The main electrodes (20) (22) are formed in a cylindrical shape or a semi-cylindrical shape, and
It may be arranged on the inner surface or the outer peripheral surface of (34).

【0026】さらに異なる実施形態として、螺旋状の羽
根を具えた筒状部材を補助電極ケースの側部に配備し、
補助電極(30)を移動させる構成とすることもできる。補
助電極ケースの下面から1つずつ補助電極(30)を筒状部
材の内部に送り込み、螺旋状の羽根の上を転動させつつ
上昇させることによって、補助電極に付着したスケール
は剥離し除去される。補助電極(30)が筒状部材の上部ま
で移動すると、補助電極(30)は筒状部材の上端から重力
作用によって補助電極ケースに落下する。補助電極(30)
は、ケース内での移動により電気的な極性が変化すると
共に、補助電極(30)(30)どうしが擦り合わされ、さら
に、筒状部材の内部を通過する間に羽根や筒状部材と接
触するから、表面にスケールが除去される。従って、補
助電極(30)を取り替えずに、長期に亘って高い電極反応
を維持することができる。
In a further different embodiment, a tubular member having spiral blades is provided on the side of the auxiliary electrode case,
The auxiliary electrode (30) may be moved. The auxiliary electrodes (30) are fed into the tubular member one by one from the lower surface of the auxiliary electrode case, and are raised while rolling on the spiral blade, whereby the scale attached to the auxiliary electrode is peeled and removed. It When the auxiliary electrode (30) moves to the upper part of the tubular member, the auxiliary electrode (30) falls from the upper end of the tubular member into the auxiliary electrode case by the action of gravity. Auxiliary electrode (30)
The electric polarity changes due to movement within the case, the auxiliary electrodes (30) and (30) are rubbed against each other, and further contact the blades and the tubular member while passing through the inside of the tubular member. The scale is removed from the surface. Therefore, a high electrode reaction can be maintained for a long period of time without replacing the auxiliary electrode (30).

【0027】<実施形態2>上記実施例では、主電極(2
0)(22)間に補助電極(30)(30)を配置し、補助電極(30)(3
0)を回転移動可能として、補助電極(30)(30)に付着する
スケールを除去したが、本実施形態では、補助電極を用
いず、主電極(20)(22)自体を移動可能な構成とし、主電
極(20)(22)の一部を順に廃水から外部に露出させ、露出
箇所に付着したスケールをスケール除去手段(76)によっ
て除去するようにしたものである。本実施形態における
電離イオン化浄化装置(10)は、浄化槽(12)の内部に一対
の主電極(20)(22)を具える。浄化槽(12)には、上記実施
形態1と同様、廃水の流入管と排水管(図示せず)を具
え、浄化槽(12)の底部にバブリング手段(13)を具える。
主電極(20)(22)は、直流電圧を印加する電源装置(18)に
接続され、主電極(20)(22)の一部が順次廃水から露出し
た状態で移動できるように、電極移動手段(70)に連繋さ
れる。主電極(20)(22)を、例えば図4に示すように円盤
状に形成して、主電極(20)(22)の一部が廃水から露出し
た状態で、主電極(20)(22)の中心に回転軸(72)(72)を連
繋し、該回転軸(72)(72)をモータ等の回転駆動手段(74)
に繋ぐ構成とすることができる。モータを駆動すると、
主電極(20)(22)は、一部が順次廃水から露出した状態で
回転する。
<Embodiment 2> In the above embodiment, the main electrode (2
Auxiliary electrodes (30) and (30) are placed between (0) and (22), and auxiliary electrodes (30) (3)
(0) can be rotationally moved to remove the scale attached to the auxiliary electrodes (30) and (30) .However, in the present embodiment, the main electrodes (20) and (22) themselves can be moved without using the auxiliary electrodes. Then, a part of the main electrodes (20) (22) is sequentially exposed from the wastewater to the outside, and the scale adhering to the exposed portions is removed by the scale removing means (76). The ionization / ionization purification device (10) in the present embodiment includes a pair of main electrodes (20) and (22) inside a septic tank (12). Similar to the first embodiment, the septic tank (12) includes a wastewater inflow pipe and a drain pipe (not shown), and the septic tank (12) has bubbling means (13) at the bottom thereof.
The main electrodes (20) (22) are connected to a power supply device (18) for applying a DC voltage, and the electrodes are moved so that a part of the main electrodes (20) (22) can be sequentially moved while being exposed from the wastewater. Connected to the means (70). The main electrodes (20) and (22) are formed in a disk shape, for example, as shown in FIG. 4, and the main electrodes (20) and (22) are partially exposed from the wastewater. ), The rotary shafts (72) and (72) are connected to each other, and the rotary shafts (72) and (72) are connected to the rotary drive means (74) such as a motor.
It can be configured to be connected to. When you drive the motor,
The main electrodes (20) and (22) rotate in a state where a part of the main electrodes is sequentially exposed from the wastewater.

【0028】主電極(20)(22)の廃水からの露出部分に
は、主電極(20)(22)に付着したスケールを除去するスケ
ール除去手段(76)が接近して配備する。スケール除去手
段(76)として、主電極(20)(22)の露出部分に向けて水を
放射する水放射手段を例示できる。主電極(20)(22)の露
出部分に水を放射することによって、表面に付着したス
ケールが剥離し、除去される。なお、露出部分だけでな
く、廃水中でのスケールの付着予防と剥離効果を高める
ために、主電極(20)(22)に超音波を照射したり、主電極
(20)(22)に向けてバブリングを施してもよい。
Scale removing means (76) for removing scale adhering to the main electrodes (20) and (22) is provided close to the exposed portions of the main electrodes (20) and (22) from the wastewater. An example of the scale removing means (76) is a water radiating means that radiates water toward the exposed portions of the main electrodes (20) and (22). By irradiating water to the exposed portions of the main electrodes (20) and (22), the scale attached to the surface is peeled off and removed. In addition to exposing the exposed parts, in order to prevent the scale from adhering to the waste water and enhance the peeling effect, the main electrodes (20) (22) are irradiated with ultrasonic waves,
Bubbling may be applied toward (20) and (22).

【0029】上記構成の電離イオン化浄化装置(10)につ
いて、流入管(14)から浄化槽(12)に廃水を導入し、バブ
リング手段(13)から廃水中に微細気泡を供給する。ま
た、主電極(20)(22)が廃水に浸漬した状態で、電源装置
(18)から直流電圧を主電極(20)(22)に印加して、回転駆
動手段(74)を駆動すると共に、スケール除去手段(76)か
ら主電極(20)(22)に向けて水を放射する。直流電圧の印
加により主電極(20)(22)間で電極反応が生じて、廃水中
の汚濁物質が凝集してフロックとなり、バブリング手段
(13)によって供給された微細気泡がフロックに吸着し
て、フロックが浮上分離し、排水管(16)から排出され
る。主電極(20)(22)に直流電圧を印加することにより、
主電極(20)(22)の表面にスケールが付着するが、主電極
(20)(22)の一部が順次廃水から露出したときに、スケー
ル除去手段(76)によって主電極(20)(22)に向けて水を放
射することによって、主電極(20)(22)に付着したスケー
ルは除去される。従って、主電極(20)(22)には、スケー
ルが堆積することなく、電極反応を進めることができ、
主電極(20)(22)を取り外して清掃したり、交換する必要
がない。なお、主電極(20)(22)の回転及びスケール除去
手段(76)の作動は、主電極(20)(22)のスケール付着具合
や廃水の汚濁程度に合わせて、連続的に行なってもよい
し、間欠的に行なってもよい。
In the ionization / ionization purification device (10) having the above structure, waste water is introduced from the inflow pipe (14) into the septic tank (12), and fine bubbles are supplied into the waste water from the bubbling means (13). Also, with the main electrodes (20) (22) immersed in wastewater,
A DC voltage is applied to the main electrodes (20) and (22) from (18) to drive the rotation driving means (74), and water is also discharged from the scale removing means (76) toward the main electrodes (20) and (22). Radiates. When a DC voltage is applied, an electrode reaction occurs between the main electrodes (20) and (22), and the pollutants in the waste water aggregate to form flocs, which causes bubbling.
The fine bubbles supplied by (13) are adsorbed on the flocs, the flocs are floated and separated, and discharged from the drain pipe (16). By applying a DC voltage to the main electrodes (20) (22),
The scale adheres to the surface of the main electrodes (20) (22),
When a part of the (20) (22) is sequentially exposed from the wastewater, the scale removing means (76) emits water toward the main electrodes (20) (22) to discharge the main electrodes (20) (22). ), The scale adhered to is removed. Therefore, the electrode reaction can proceed without depositing scale on the main electrodes (20) (22),
There is no need to remove, clean or replace the main electrodes (20) (22). The rotation of the main electrodes (20) (22) and the operation of the scale removing means (76) may be continuously performed depending on the scale attachment degree of the main electrodes (20) (22) and the degree of pollution of waste water. You may do it intermittently.

【0030】上記実施形態2では、実施形態1の補助電
極(30)(30)を用いていないが、主電極(20)(22)間に補助
電極を移動可能に配備して、主電極(20)(22)だけでな
く、補助電極によっても電極反応を進めることによっ
て、効率よく汚濁物質を除去できる。
In the second embodiment, the auxiliary electrodes (30) and (30) of the first embodiment are not used, but the auxiliary electrodes are movably arranged between the main electrodes (20) and (22) to Not only 20) and 22), the pollutant can be efficiently removed by promoting the electrode reaction not only by the auxiliary electrode.

【0031】[0031]

【実施例】<実施例1>図1に示す実施形態1の電離イ
オン化浄化装置(10)を用い、廃水(以下原水A〜Dとい
う)の浄化を試みた。なお、補助電極(30)(30)は、直径
3〜5cmの球状のものを80個投入した。 [その他条件] 原水の量:10リットル 処理時間:60分 電圧値:30V 電流値:2A
EXAMPLES Example 1 An attempt was made to purify wastewater (hereinafter referred to as raw water A to D) using the ionization / ionization purification apparatus (10) of Embodiment 1 shown in FIG. As the auxiliary electrodes (30) and (30), 80 spherical electrodes having a diameter of 3 to 5 cm were put. [Other conditions] Amount of raw water: 10 liters Processing time: 60 minutes Voltage value: 30V Current value: 2A

【0032】なお、原水A〜Dについて、外観と臭いを
調べたところ、以下のような結果であった。 原水A:見た目は澄んだきれい。臭いもない。 原水B:茶色く濁っている。エビの腐敗臭が強い。 原水C:薄茶色に濁っている。僅かにエビの腐敗臭があ
る。 原水D:薄黄色く濁っている。僅かに臭いがある。 また、原水A〜Dについて、リン濃度を調べたところ表
1に示す結果であった。
When the appearance and odor of raw water A to D were examined, the following results were obtained. Raw water A: It looks clear and beautiful. There is no odor. Raw water B: Brown and cloudy. The rotten smell of shrimp is strong. Raw water C: Light brown and cloudy. There is a slight rotten smell of shrimp. Raw water D: Light yellow and cloudy. There is a slight odor. Further, when the phosphorus concentrations of the raw waters A to D were examined, the results shown in Table 1 were obtained.

【0033】[0033]

【表1】 [Table 1]

【0034】原水A〜Dを本発明の電離イオン化浄化装
置(10)を用いて浄化した結果を表1に示している。
Table 1 shows the results of purification of raw water A to D using the ionization / ionization purification apparatus (10) of the present invention.

【0035】表1を参照すると、浄化水A〜Dは浄化後
のリン濃度がすべて低下しており、除去率が非常に高い
ことが判る。これは、主電極(20)(22)だけでなく、主電
極(20)(22)間に配置された補助電極(30)(30)による電極
反応によって、効果的にリンが除去されたことを示して
いる。
Referring to Table 1, it is understood that the purified waters A to D all have a reduced phosphorus concentration after purification, and that the removal rates are very high. This is because phosphorus was effectively removed not only by the main electrodes (20) (22) but also by the electrode reaction caused by the auxiliary electrodes (30) (30) arranged between the main electrodes (20) (22). Is shown.

【0036】上記処理をリン濃度の高いその他の原水に
施したところ、リン濃度は、原水23ppmから浄化水
0.14ppmと同様に低減できた。
When the above treatment was applied to other raw water having a high phosphorus concentration, the phosphorus concentration could be reduced from 23 ppm of the raw water to 0.14 ppm of the purified water.

【0037】<実施例2>図1に示すように、主電極(2
0)(22)間に補助電極(30)(30)を移動可能に配置した本発
明の電離イオン化浄化装置(10)と、図5に示すように、
主電極(92)(94)間に補助電極を具えていない浄化装置(1
0)を作製し、CODの高い廃水(糖分を多量に含んだC
ODの高い廃水)を用いて、直流電圧30Vを印加し浄
化運転を行なった。浄化運転開始直後の主電極間の電流
値は共に約2Aであった。その後、経時的に主電極間の
電流値を測定したところ、本発明の浄化装置(10)は、2
ヶ月経過しても主電極(20)(22)間に流れる電流を約2A
に維持できた。これは、補助電極(30)(30)の転動による
極性変化と、補助電極(30)(30)どうしがぶつかり合うこ
とによって、表面にスケールが付着するのを防止できた
ためである。一方、比較例の浄化装置は、3日で電流値
が約0.1〜0.3Aに低下し、1週間で殆んど電流が流
れなくなり、主電極(92)(94)を廃水から取り出してみる
と、主電極の周りにスケールが固まった状態で付着して
いた。
Example 2 As shown in FIG. 1, the main electrode (2
As shown in FIG. 5, an ionization / ionization purification device (10) of the present invention in which auxiliary electrodes (30) and (30) are movably arranged between 0 and (22).
Purification device (1) that does not have an auxiliary electrode between the main electrodes (92) and (94)
0) was produced and wastewater with high COD (C containing a large amount of sugar
Wastewater with high OD) was used to apply a DC voltage of 30 V to carry out purification operation. Immediately after the start of the cleaning operation, the current values between the main electrodes were both about 2A. After that, when the current value between the main electrodes was measured with time, the purification device (10) of the present invention showed that
The current flowing between the main electrodes (20) and (22) is about 2A even after a lapse of months.
I was able to maintain. This is because it is possible to prevent the scale from adhering to the surface due to the collision between the auxiliary electrodes (30, 30) and the change in polarity due to the rolling of the auxiliary electrodes (30, 30). On the other hand, in the purification device of the comparative example, the current value dropped to about 0.1 to 0.3 A in 3 days, and almost no current flowed in 1 week, and the main electrodes (92) (94) were taken out from the wastewater. As a result, the scale was adhered around the main electrode in a solidified state.

【0038】上記実施例の説明は、本発明を説明するた
めのものであって、特許請求の範囲に記載の発明を限定
し、或は範囲を減縮する様に解すべきではない。又、本
発明の各部構成は上記実施例に限らず、特許請求の範囲
に記載の技術的範囲内で種々の変形が可能である。
The above description of the embodiments is for explaining the present invention, and should not be construed as limiting the invention described in the claims or reducing the scope. Further, the configuration of each part of the present invention is not limited to the above embodiment, but various modifications can be made within the technical scope described in the claims.

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

【図1】本発明の実施形態1の電離イオン化浄化装置の
斜視図である。
FIG. 1 is a perspective view of an ionization / ionization purification device according to a first embodiment of the present invention.

【図2】本発明の電離イオン化浄化装置を具えた浄化シ
ステムを示す説明図である。
FIG. 2 is an explanatory diagram showing a purification system including the ionization / ionization purification device of the present invention.

【図3】電離イオン化浄化装置の他の実施形態を示す説
明図である。
FIG. 3 is an explanatory view showing another embodiment of the ionization / ionization purification device.

【図4】本発明の実施形態2の電離イオン化浄化装置の
斜視図である。
FIG. 4 is a perspective view of an ionization / ionization purification device according to a second embodiment of the present invention.

【図5】従来の浄化装置の断面図である。FIG. 5 is a cross-sectional view of a conventional purification device.

【符号の説明】[Explanation of symbols]

(10) 電離イオン化浄化装置 (12) 浄化槽 (20) 主電極 (22) 主電極 (30) 補助電極 (34) ケース (10) Ionization and purification device (12) Septic tank (20) Main electrode (22) Main electrode (30) Auxiliary electrode (34) Case

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 廃水を含む浄化槽中に配置された電極に
直流電圧を印加することによって、廃水中の汚濁物質を
除去する電離イオン化浄化装置において、 電極を移動可能に配備し、電極を回転させつつ移動させ
ることによって該電極表面に付着したスケールを除去で
きるようにしたことを特徴とする電離イオン化浄化装
置。
1. In an ionization / ionization purification device for removing pollutants in wastewater by applying a DC voltage to the electrode arranged in a septic tank containing wastewater, the electrode is movably arranged and the electrode is rotated. An ionization / ionization purification device characterized in that the scale attached to the surface of the electrode can be removed by moving the electrode while moving it.
【請求項2】 廃水を含む浄化槽中に配置された一対の
電極間に直流電圧を印加することによって、廃水中の汚
濁物質を除去する電離イオン化浄化装置において、 電極間に複数の補助電極を回転移動可能に配備し、補助
電極を回転させつつ移動させることにより補助電極の表
面に付着したスケールを除去するようにしたことを特徴
とする電離イオン化浄化装置。
2. An ionization / ionization purification apparatus for removing contaminants in wastewater by applying a DC voltage between a pair of electrodes arranged in a septic tank containing wastewater, and rotating a plurality of auxiliary electrodes between the electrodes. An ionization and ionization purification device characterized in that it is movably arranged and scales attached to the surface of the auxiliary electrode are removed by moving the auxiliary electrode while rotating it.
【請求項3】 電極間には、内部に廃水が流通可能な補
助電極ケースが回転可能に配備されており、補助電極
は、補助電極ケースに収容され、補助電極ケースを回転
させることによって、補助電極が補助電極ケース内で回
転しつつ移動し、補助電極の表面に付着したスケールが
電気的に除去される請求項2に記載の電離イオン化浄化
装置。
3. An auxiliary electrode case in which waste water can flow is disposed rotatably between the electrodes, and the auxiliary electrode is housed in the auxiliary electrode case and is rotated by rotating the auxiliary electrode case. The ionization / purification device according to claim 2, wherein the electrode moves while rotating in the auxiliary electrode case, and the scale attached to the surface of the auxiliary electrode is electrically removed.
【請求項4】 電極間には、内部に廃水が流通可能な補
助電極ケースが配備されており、補助電極は、補助電極
ケースに収容され、補助電極ケースの下面には、補助電
極を移動させる撹拌部材を具え、撹拌部材を回転させる
ことによって、内部に収容された補助電極が回転しつつ
移動し、補助電極の表面に付着したスケールが電気的に
除去される請求項2に記載の電離イオン化浄化装置。
4. An auxiliary electrode case in which wastewater can flow is provided between the electrodes, the auxiliary electrode is housed in the auxiliary electrode case, and the auxiliary electrode is moved to the lower surface of the auxiliary electrode case. The ionization ionization according to claim 2, further comprising a stirring member, and by rotating the stirring member, the auxiliary electrode housed inside moves while rotating, and the scale attached to the surface of the auxiliary electrode is electrically removed. Purification device.
【請求項5】 廃水を含む浄化槽中に配置された一対の
電極間に直流電圧を印加することによって、廃水中の汚
濁物質を除去する電離イオン化浄化装置において、 電極の一部を順次廃水から露出するように電極を移動可
能に支持する電極移動手段と、 電極の露出部分に付着したスケールを除去するスケール
除去手段とを具えることを特徴とする電離イオン化浄化
装置。
5. An ionization and ionization purification device for removing pollutants in wastewater by applying a DC voltage between a pair of electrodes arranged in a septic tank containing wastewater, and a part of the electrodes is exposed sequentially from the wastewater. An ionization / ionization purification apparatus comprising: an electrode moving unit that movably supports the electrode, and a scale removing unit that removes scale attached to an exposed portion of the electrode.
JP2002098177A 2002-04-01 2002-04-01 Ionization and ionization purification equipment Expired - Fee Related JP3692327B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002098177A JP3692327B2 (en) 2002-04-01 2002-04-01 Ionization and ionization purification equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002098177A JP3692327B2 (en) 2002-04-01 2002-04-01 Ionization and ionization purification equipment

Publications (2)

Publication Number Publication Date
JP2003290773A true JP2003290773A (en) 2003-10-14
JP3692327B2 JP3692327B2 (en) 2005-09-07

Family

ID=29240287

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002098177A Expired - Fee Related JP3692327B2 (en) 2002-04-01 2002-04-01 Ionization and ionization purification equipment

Country Status (1)

Country Link
JP (1) JP3692327B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011031193A (en) * 2009-08-03 2011-02-17 Mitsubishi Electric Corp Scale removal device
KR101221565B1 (en) 2010-07-28 2013-01-14 정해웅 Electrolytic treatment of waste water
US20140001120A1 (en) * 2012-06-28 2014-01-02 Rowanwood Ip Inc. Removal of phosphorus from sewage by electrode metal addition
JP2016123962A (en) * 2015-01-07 2016-07-11 株式会社アルファ技研 Water treatment equipment, cooling tower and cooling tower system
JP6235752B1 (en) * 2017-07-28 2017-11-22 株式会社アルファ技研 Water treatment equipment, cooling tower and cooling tower system

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011031193A (en) * 2009-08-03 2011-02-17 Mitsubishi Electric Corp Scale removal device
KR101221565B1 (en) 2010-07-28 2013-01-14 정해웅 Electrolytic treatment of waste water
US20140001120A1 (en) * 2012-06-28 2014-01-02 Rowanwood Ip Inc. Removal of phosphorus from sewage by electrode metal addition
US10787377B2 (en) 2012-06-28 2020-09-29 Waterloo Biofilter Systems Inc. Removal of phosphorus from sewage by electrode metal addition
JP2016123962A (en) * 2015-01-07 2016-07-11 株式会社アルファ技研 Water treatment equipment, cooling tower and cooling tower system
JP6235752B1 (en) * 2017-07-28 2017-11-22 株式会社アルファ技研 Water treatment equipment, cooling tower and cooling tower system
WO2019021633A1 (en) * 2017-07-28 2019-01-31 株式会社アルファ技研 Water processing device, cooling tower, and cooling tower system
JP2019025408A (en) * 2017-07-28 2019-02-21 株式会社アルファ技研 Water treatment device, cooling tower and cooling tower system

Also Published As

Publication number Publication date
JP3692327B2 (en) 2005-09-07

Similar Documents

Publication Publication Date Title
US8551305B2 (en) Apparatus for treating water or wastewater
CN102936072B (en) Nano-catalysis, electrolysis, flocculation and air-floatation device
CN102596077B (en) Turboelectric coagulation apparatus
JP2005000858A (en) Photocatalytic water treatment apparatus
CN205313291U (en) Refrigeration cycle water integrated processing system
KR101702345B1 (en) Apparatus and Method for Removing Algae
KR200191269Y1 (en) Ultrasonic wave device for waste water treatment using hollow fiber filter
CN202519115U (en) Nano-catalysis, electrolysis, flocculation and air-floatation device
CN110482809B (en) Method and device for electrochemically enhancing sludge concentration and synchronously removing heavy metals
JPH10118390A (en) Washing machine with electrolytic waste water treating device
JP3692327B2 (en) Ionization and ionization purification equipment
CN209853950U (en) A sewage treatment plant for circuit board workshop
CN205313294U (en) But continuous operation&#39;s cooling circulating water treatment system
US6428697B1 (en) System for processing waste water
KR101913754B1 (en) Apparatus of solid-liquid separation comprising settling tank and floatation separation tank and method using the same
CN113087263B (en) Zero release sewage treatment system
CN106145270B (en) Electrolytic sewage purifying processing device and electrolytic sewage purification system
CN200943048Y (en) Foodstuff pickling waste water purification treating apparatus
WO2013075240A1 (en) Treatment of a waste stream through production and utilization of oxyhydrogen gas
JP4049711B2 (en) Wastewater treatment method including ethylene carbonate
JP4549000B2 (en) Water purification equipment for suspended solids
KR20030068083A (en) Waste water disposal apparatus having a scale removing means
JP2001347295A (en) Apparatus for cleaning seawater containing floating substance
RU2813075C1 (en) Method for purification of waste and produced water
CN110845058B (en) Sewage treatment method based on electrochemistry

Legal Events

Date Code Title Description
A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20040921

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20041112

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20050104

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20050303

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20050531

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20050620

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090624

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090624

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100624

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110624

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120624

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130624

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140624

Year of fee payment: 9

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees
R154 Certificate of patent or utility model (reissue)

Free format text: JAPANESE INTERMEDIATE CODE: R154