JP2001300536A - Waste water treating device - Google Patents

Waste water treating device

Info

Publication number
JP2001300536A
JP2001300536A JP2000118203A JP2000118203A JP2001300536A JP 2001300536 A JP2001300536 A JP 2001300536A JP 2000118203 A JP2000118203 A JP 2000118203A JP 2000118203 A JP2000118203 A JP 2000118203A JP 2001300536 A JP2001300536 A JP 2001300536A
Authority
JP
Japan
Prior art keywords
wastewater
electrode
wastewater treatment
treated
treatment tank
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
JP2000118203A
Other languages
Japanese (ja)
Inventor
Yorihiko Yamashita
偉彦 山下
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 JP2000118203A priority Critical patent/JP2001300536A/en
Priority to KR1020010021258A priority patent/KR20010098763A/en
Publication of JP2001300536A publication Critical patent/JP2001300536A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • C02F2001/46152Electrodes characterised by the shape or form
    • C02F2001/46171Cylindrical or tubular shaped

Abstract

PROBLEM TO BE SOLVED: To provide a waste water treating device in which a treating tank is manufactured so as to have a hermetically sealed structure at a low cost. SOLUTION: A waste water treating tank 10 is constituted such that a second electrode 12 is housed with a specified spacing in a first electrode 11 having a nearly hermetically sealed hollow shape, and the second electrode 12 is supported by the first electrode 11 via an insulator, and waste water is allowed to flow between the first electrode 11 and the second electrode 12. The first electrode 11 is tubular, preferably cylindrical, and the second electrode 12 is tubular or has a cylinder shape, preferably cylindrical or a cylinder shape being circular in the cross-section.

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】本発明は廃水処理装置に関
し、特に処理槽に密閉構造を採用でき、しかも安価に製
作できるようにした装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a wastewater treatment apparatus, and more particularly to an apparatus capable of adopting a closed structure in a treatment tank and being manufactured at a low cost.

【0002】[0002]

【従来の技術】生活系廃水や産業系廃水等を処理する場
合、微生物を用いる生物処理法と、電気エネルギーを用
いる電解法とが一般的に採用されている。
2. Description of the Related Art When treating domestic wastewater or industrial wastewater, a biological treatment method using microorganisms and an electrolysis method using electric energy are generally employed.

【0003】後者の電解法は廃水に電気エネルギーを与
えることにより、電極面と廃水の接触界面に生ずる反応
や析出物質と廃水中の成分との間に生ずる吸着反応、具
体的には電気分解、電気析出、電解酸化、電解還元、電
解中和、イオン交換等の電気反応を利用し、廃水の高分
子無機物や高分子有機物を低分子化し、BODやCOD
を低下させる方法であり、エネルギー源としての電源を
必要とするものの、前者の生物処理方法に比してメンテ
ナンスが容易であるという利点がある。
In the latter electrolysis method, by applying electric energy to wastewater, a reaction occurring at a contact interface between an electrode surface and the wastewater or an adsorption reaction occurring between a deposited substance and a component in the wastewater, specifically, electrolysis, Utilizing electric reactions such as electro-deposition, electrolytic oxidation, electrolytic reduction, electrolytic neutralization, and ion exchange, the polymer inorganic matter and polymer organic matter in wastewater are reduced to low molecular weight, and BOD and COD
Although this method requires a power source as an energy source, it has an advantage that maintenance is easier than the former biological treatment method.

【0004】従来、かかる電解法では平坦な複数の陽極
板と陰極板を処理槽内に適切な間隔をあけて交互に配置
した方式が広く採用されていた(例えば、特開昭55−
127189号公報、特開平06−296805号公
報、特開平06−304406号公報、等参照)。
Heretofore, in such an electrolysis method, a system in which a plurality of flat anode plates and cathode plates are alternately arranged at appropriate intervals in a treatment tank has been widely adopted (for example, Japanese Patent Laid-Open No. 55-55).
127189, JP-A-06-296805, JP-A-06-304406, etc.).

【0005】[0005]

【発明が解決しようとする課題】しかし、従来の方式で
は廃水中に塩素系成分等が含まれていると、塩素ガス等
の有害なガスが生成して雰囲気を汚染するばかりでな
く、通電線を接続する電極の端子が腐食しやすいという
問題があった。
However, in the conventional method, when chlorine-based components and the like are contained in wastewater, not only harmful gases such as chlorine gas are generated to pollute the atmosphere, but also the electric current There is a problem that the terminals of the electrodes connecting the electrodes are easily corroded.

【0006】これに対し、処理槽を密閉構造にし、塩素
ガスを廃水中に溶け込ませる方法が提案されているが、
処理槽に耐圧容器を採用する必要があり、コスト高を招
来するばかりでなく、電極端子の処理槽への支持構造が
複雑になり、設備メインテナンスが非常に煩雑になると
いう問題がある。
On the other hand, a method has been proposed in which the treatment tank is made to have a closed structure and chlorine gas is dissolved in wastewater.
It is necessary to employ a pressure-resistant container for the processing tank, which not only causes an increase in cost, but also has a problem that the structure for supporting the electrode terminals in the processing tank is complicated, and equipment maintenance becomes very complicated.

【0007】本発明はかかる問題点に鑑み、雰囲気の汚
染や電極端子の腐食を発生させることがなく、しかも構
造簡単で安価に製作できるようにした廃水処理装置を提
供することを課題とする。
SUMMARY OF THE INVENTION In view of the above problems, an object of the present invention is to provide a wastewater treatment apparatus which does not cause pollution of the atmosphere or corrosion of electrode terminals, and which can be manufactured simply and at low cost.

【0008】[0008]

【課題を解決するための手段】そこで、本発明に係る廃
水処理装置は、廃水に電気エネルギーを与えて処理を行
う廃水処理装置において、ほぼ密閉した中空状の第1の
電極内に第2の電極を所定の隙間をあけて収容するとと
もに該第2の電極を上記第1の電極に対して絶縁材を介
して支持して構成されてなる廃水処理槽と、該廃水処理
槽の第1、第2の電極の間に電流を通電する通電手段
と、上記廃水処理槽に設けられ、上記第1の電極と第2
の電極との間に処理すべき廃水を流入させる廃水流入口
と、上記廃水処理槽に設けられ、上記第1の電極と第2
の電極との間で処理された廃水を排出する処理済み廃水
排出口と、上記廃水流入口に接続された廃水供給通路
と、該廃水供給通路に廃水を加圧して供給する加圧手段
と、上記処理済み廃水排出口に接続された排出通路と、
を備えたことを特徴とする。
SUMMARY OF THE INVENTION Therefore, a wastewater treatment apparatus according to the present invention is a wastewater treatment apparatus for performing treatment by applying electric energy to wastewater. A wastewater treatment tank configured to house the electrodes with a predetermined gap therebetween and to support the second electrode with respect to the first electrode via an insulating material; An energizing means for applying an electric current between the second electrodes; and
A wastewater inlet through which wastewater to be treated flows between the first electrode and the second electrode;
A treated wastewater outlet for discharging wastewater treated between the electrodes, a wastewater supply passage connected to the wastewater inlet, and a pressurizing means for supplying wastewater to the wastewater supply passage by pressurizing the wastewater, A discharge passage connected to the treated wastewater discharge port,
It is characterized by having.

【0009】本発明の特徴の1つは第1の電極をほぼ密
閉した中空状に形成し、第1の電極内に第2の電極を挿
入して廃水処理槽を構成するようにした点にある。これ
により、廃水中に塩素系成分等が含まれている場合にも
生成した塩素ガス等の有害なガスがそのまま環境に放出
されるおそれもなく、又電極の接続端子が腐食すること
もない。
One of the features of the present invention is that the first electrode is formed in a substantially closed hollow shape, and the second electrode is inserted into the first electrode to constitute a wastewater treatment tank. is there. Thus, even when the wastewater contains a chlorine-based component or the like, no harmful gas such as generated chlorine gas is released to the environment as it is, and the connection terminals of the electrodes are not corroded.

【0010】また、廃水処理槽自体を電極としているの
で、処理槽に耐圧容器を採用する場合のようにコスト高
を招来することがなく、又第2の電極を第1の電極に対
して絶縁材を介して接続すればよいので、電極の支持構
造も簡単になり、設備メインテナンスも大幅に簡素化で
きる。
In addition, since the wastewater treatment tank itself is used as an electrode, the cost does not increase as in the case of using a pressure-resistant container for the treatment tank, and the second electrode is insulated from the first electrode. Since the connection can be made via the material, the electrode support structure can be simplified, and equipment maintenance can be greatly simplified.

【0011】また、廃水を加圧して生成ガスを廃水中に
溶け込ませるようにしているので、ガスと廃水との接触
が容易である。この場合、廃水の加圧は所定圧力に一定
に制御するようにしてもよいが、圧力変動させることも
できる。但し、廃水を常に加圧すると、廃水中に酸素以
外のガスも溶解し、ほぼ飽和状態となり、反応効率が低
下する。酸素以外のガスが廃水中に存在すると、酸素と
処理物質との反応が悪くなると考えられる。そこで、加
圧力を一定時間毎に又は間欠的に変動させて一旦常圧に
戻すと、廃水に溶解しているガスが気化して外部に排気
をし、改めて発生させた酸素とで廃水中の結合を促すこ
とができる。
Further, since the waste gas is pressurized and the produced gas is dissolved in the waste water, the gas and the waste water can be easily contacted. In this case, the pressurization of the wastewater may be controlled to be constant at a predetermined pressure, but the pressure may be varied. However, if the wastewater is constantly pressurized, gases other than oxygen are also dissolved in the wastewater, and the wastewater is almost saturated, and the reaction efficiency is reduced. If a gas other than oxygen is present in the wastewater, it is considered that the reaction between oxygen and the treatment substance is deteriorated. Therefore, if the pressure is changed to a normal pressure once or intermittently at regular intervals, the gas dissolved in the wastewater is vaporized and exhausted to the outside, and the oxygen in the wastewater is regenerated with oxygen newly generated. It can encourage binding.

【0012】即ち、加圧手段は廃水に対して所定の一定
圧を加圧するようになしてもよく、又廃水に対する加圧
力を変動させるようになしてもよい。
That is, the pressurizing means may pressurize the wastewater at a predetermined constant pressure, or may vary the pressure applied to the wastewater.

【0013】廃水処理槽は一槽だけ設けてバッチ式に廃
水処理することもできるが、大量の廃水を効率よく処理
する場合には複数の廃水処理槽を設けて連続式に処理す
ることもできる。
A single wastewater treatment tank can be provided for batchwise wastewater treatment. However, if a large amount of wastewater is to be treated efficiently, a plurality of wastewater treatment tanks can be provided for continuous treatment. .

【0014】即ち、複数の廃水処理槽を設け、複数の各
廃水処理槽の排出通路には次の廃水処理槽の廃水供給通
路を順次接続することにより、複数の廃水処理槽を直列
に接続して廃水処理槽群を構成するのがよい。
That is, a plurality of wastewater treatment tanks are provided, and a plurality of wastewater treatment tanks are connected in series by sequentially connecting a wastewater supply passage of the next wastewater treatment tank to a discharge passage of each of the plurality of wastewater treatment tanks. To form a wastewater treatment tank group.

【0015】また、廃水処理槽を出た処理済みの廃水は
そのまま次の工程に移行させてもよいが、廃水をより完
全に処理する上で、処理済みの廃水の一部を廃水処理槽
に戻して処理させることもできる。
[0015] The treated wastewater leaving the wastewater treatment tank may be directly transferred to the next step. However, in order to more completely treat the wastewater, a part of the treated wastewater is transferred to the wastewater treatment tank. It can be returned and processed.

【0016】即ち、廃水供給通路と排出通路との間には
廃水循環通路を接続し、廃水循環通路には排出通路内の
処理済み廃水の一部を廃水供給通路に循環させる循環ポ
ンプを設けるようにするのがよい。
That is, a wastewater circulation passage is connected between the wastewater supply passage and the discharge passage, and the wastewater circulation passage is provided with a circulation pump for circulating a part of the treated wastewater in the discharge passage to the wastewater supply passage. It is better to

【0017】本発明に係る廃水処理装置は新規でかつ斬
新であるが、かかる廃水処理装置に採用される廃水処理
槽も新規かつ斬新であり、本発明によればかかる廃水処
理槽を提供することができる。
Although the wastewater treatment apparatus according to the present invention is new and novel, the wastewater treatment tank employed in such a wastewater treatment apparatus is also novel and novel, and the present invention provides such a wastewater treatment tank. Can be.

【0018】本発明に係る廃水処理槽は、長手方向にほ
ぼ均一な内径を有する筒状をなし、ほぼ密閉構造の第1
の電極と、長手方向にほぼ均一な外径を有する筒状又は
棒状をなし、上記第1の電極内に所定の隙間をあけて収
容され、上記第1の電極に絶縁部材を介して支持された
第2の電極と、上記第1の電極と第2の電極との間に処
理すべき廃水を流入させる廃水流入口と、上記第1の電
極と第2の電極との間で処理された廃水を排出する処理
済み廃水排出口とを備えたことを特徴とする。
The wastewater treatment tank according to the present invention has a cylindrical shape having a substantially uniform inner diameter in the longitudinal direction, and has a substantially closed structure.
And a cylindrical or rod-like shape having a substantially uniform outer diameter in the longitudinal direction, accommodated in the first electrode with a predetermined gap, and supported by the first electrode via an insulating member. A second electrode, a wastewater inlet through which wastewater to be treated flows between the first electrode and the second electrode, and a wastewater inlet treated between the first electrode and the second electrode. And a treated wastewater discharge port for discharging wastewater.

【0019】廃水に電気エネルギーを与えて処理する場
合、電極面から3mm以上離れた箇所においては廃水の
処理効率が低下し、廃水が処理されないで流通するおそ
れがある。従って、廃水を効率よく処理するためには電
極を所定の狭い寸法に精度よく、しかも相互に平行に保
持されることが望ましい。しかし、従来の廃水処理シス
テムのように平板状の電極を採用した場合には隣接する
電極板を相互に平行に維持するのが難しい。本発明にお
いては第1の電極を筒状に、第2の電極を筒状又は棒状
に形成しているので、第1、第2の電極を所定の狭い間
隔に高精度にかつ相互に平行に保持することができる。
When the wastewater is treated with electric energy, the treatment efficiency of the wastewater is reduced at a position distant from the electrode surface by 3 mm or more, and the wastewater may flow without being treated. Therefore, in order to treat wastewater efficiently, it is desirable that the electrodes be held in a predetermined narrow dimension with high precision and parallel to each other. However, when flat electrodes are employed as in a conventional wastewater treatment system, it is difficult to keep adjacent electrode plates parallel to each other. In the present invention, since the first electrode is formed in a cylindrical shape and the second electrode is formed in a cylindrical or rod-like shape, the first and second electrodes are formed at a predetermined narrow interval with high precision and parallel to each other. Can be held.

【0020】第1、第2の電極は四角筒状、その他の多
角筒状としてもよいが、円筒状とすると、第1、第2の
電極をより簡単にかつ相互に平行に組立てることができ
る。即ち、第1、第2の電極を円筒状となし、第1、第
2の電極の中心軸線を一致させて両電極を配置すると、
両者の平行度をより正確に保証できる。
The first and second electrodes may have a rectangular cylindrical shape or another polygonal cylindrical shape, but if they are cylindrical, the first and second electrodes can be assembled more easily and in parallel with each other. . That is, when the first and second electrodes are formed in a cylindrical shape, and the first and second electrodes are arranged so that the central axes thereof are aligned with each other,
The parallelism between the two can be more accurately guaranteed.

【0021】廃水流入口及び処理済み廃水排出口は第
1、第2の電極の間に処理すべき廃水が流通できればど
のように設けてもよいが、上述のように筒状又は円筒状
の第1、第2の電極を採用する場合、第2の電極の一端
を開口して廃水導入口又は処理済み廃水排出口とするの
がよい。
The wastewater inlet and the treated wastewater outlet may be provided in any manner as long as the wastewater to be treated can flow between the first and second electrodes. When employing the first and second electrodes, one end of the second electrode is preferably opened to serve as a wastewater inlet or a treated wastewater outlet.

【0022】即ち、第2の電極の一端を開口して廃水流
入口となす一方、第2の電極の他端側には廃水導入口を
形成し、第1の電極には処理済み廃水排出口を廃水導入
口から導入された廃水を第1、第2の電極の間に流通さ
せるように形成することができる。
That is, one end of the second electrode is opened to form a wastewater inlet, while the other end of the second electrode is formed with a wastewater inlet, and the first electrode is a treated wastewater outlet. Can be formed so that the wastewater introduced from the wastewater introduction port flows between the first and second electrodes.

【0023】また、第2の電極の一端を開口して処理済
み廃水排出口となす一方、第2の電極の他端側には廃水
導入口を形成し、第1の電極には廃水流入口を第1、第
2の電極間を流通した廃水を廃水導入口から第2の電極
内に導入させるように形成することもできる。
In addition, one end of the second electrode is opened to form a treated wastewater discharge port, while a wastewater inlet is formed at the other end of the second electrode, and a wastewater inlet is formed at the first electrode. Can be formed so that the wastewater flowing between the first and second electrodes is introduced into the second electrode from the wastewater inlet.

【0024】また、第2の電極を筒状ではなく、棒状と
する場合、第1、第2の電極の電極面の高い平行度を確
保する上で、第1の電極が円筒状をなし、第2の電極が
断面円形の棒状をなし、上記第1、第2の電極が中心軸
線を一致させて配置されるのがよい。
When the second electrode is not cylindrical but rod-shaped, the first electrode has a cylindrical shape in order to ensure high parallelism between the electrode surfaces of the first and second electrodes. Preferably, the second electrode has a rod shape with a circular cross section, and the first and second electrodes are arranged so that their central axes coincide.

【0025】また、棒状の第2の電極を採用する場合、
第1の電極の一端側には廃水流入口を、第1の電極の他
端側には処理済み廃水排出口を各々形成するのがよい
が、かかる構造は上述の筒状の第2の電極を採用する場
合にも同様に適用できる。
When a rod-shaped second electrode is employed,
It is preferable to form a wastewater inlet at one end of the first electrode and a treated wastewater outlet at the other end of the first electrode. The same can be applied to the case where is adopted.

【0026】[0026]

【発明の実施の形態】以下、本発明を図面に示す具体例
に基づいて詳細に説明する。図1は本発明に係る廃水処
理装置の好ましい実施形態を示す。図において、廃水処
理槽10は第1の電極11と第2の電極12とを組合せ
てほぼ密閉構造に構成されている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail with reference to specific examples shown in the drawings. FIG. 1 shows a preferred embodiment of the wastewater treatment apparatus according to the present invention. In the figure, a wastewater treatment tank 10 is configured in a substantially closed structure by combining a first electrode 11 and a second electrode 12.

【0027】第1の電極11は長手方向に均一な内外径
を有するステンレス鋼製の円形パイプを用いて製作され
ている。この第1の電極11の上端には電極の一部を構
成する筒状金具13が嵌め込まれ、筒状金具13には処
理済み廃水排出口14が形成されている。
The first electrode 11 is manufactured using a stainless steel circular pipe having a uniform inner and outer diameter in the longitudinal direction. A cylindrical fitting 13 constituting a part of the electrode is fitted into the upper end of the first electrode 11, and a treated wastewater discharge port 14 is formed in the tubular fitting 13.

【0028】この筒状金具13の上端には変形筒状の支
持金具15が連結片16によって連結され、支持金具1
5の上端には金属製の封鎖片17が嵌め込まれている。
A deformable cylindrical support member 15 is connected to the upper end of the cylindrical member 13 by a connecting piece 16.
A metal sealing piece 17 is fitted into the upper end of 5.

【0029】他方、第2の電極12は第1の電極11よ
りも小径でかつ長手方向にほぼ均一な内外径を有するス
テンレス鋼製の円形パイプを用いて製作され、第2の電
極12は第1の電極11内に挿入され、第2の電極12
の上方部分は第1の電極11から突設されている。
On the other hand, the second electrode 12 is manufactured using a stainless steel circular pipe having a smaller diameter than the first electrode 11 and having a substantially uniform inner and outer diameter in the longitudinal direction. One electrode 11 is inserted into the second electrode 12
Is projected from the first electrode 11.

【0030】この第2の電極12と封鎖片17との間に
は合成樹脂製の筒体(絶縁材)18が介設され、該筒体
18はOリング19によって抜け止めされ、Oリング1
9の上方には合成樹脂製のキャップ20が嵌め込まれて
おり、こうして第1の電極11の上方側は密閉されてい
る。
A cylindrical body (insulating material) 18 made of synthetic resin is interposed between the second electrode 12 and the sealing piece 17, and the cylindrical body 18 is prevented from coming off by an O-ring 19,
A cap 20 made of a synthetic resin is fitted above 9, and thus the upper side of the first electrode 11 is sealed.

【0031】また、第2の電極12の上端にはチタン製
パイプ21が筒体18内において連結され、チタン製パ
イプ21の上端は開口されて廃水流入口となっている。
この廃水流入口には筒状の連結部材22が連結され、連
結ブラケット22には廃水供給パイプ(廃水供給通路)
23の一端が連結され、廃水供給パイプ23の他端側に
は加圧ポンプ(加圧手段)24が介設され、廃水供給パ
イプ23の他端は廃水タンク25に至っている。
A titanium pipe 21 is connected to the upper end of the second electrode 12 in the cylindrical body 18, and the upper end of the titanium pipe 21 is opened to serve as a wastewater inlet.
A cylindrical connecting member 22 is connected to the wastewater inlet, and a wastewater supply pipe (wastewater supply passage) is connected to the connection bracket 22.
One end of the wastewater supply pipe 23 is connected, and a pressurizing pump (pressurizing means) 24 is interposed at the other end of the wastewater supply pipe 23, and the other end of the wastewater supply pipe 23 reaches a wastewater tank 25.

【0032】また、第2の電極12の下端側には廃水導
入口26が開口され、第2の電極12内を流通してきた
廃水を第1、第2の電極11、12間に導入するように
なっている。
A waste water inlet 26 is opened at the lower end of the second electrode 12 so that waste water flowing through the second electrode 12 is introduced between the first and second electrodes 11 and 12. It has become.

【0033】他方、第1の電極11の下端には合成樹脂
製の密閉蓋27が嵌め込まれ、第1、第2の電極11、
12の下端部の間には合成樹脂製のスペーサ(絶縁材)
28が介設され、こうして第1、第2の電極11、12
は両者の中心軸線を一致させかつ両者の間に所定の隙
間、例えば約3mmの隙間を長手方向にほぼ均等にあけ
て配置されている。
On the other hand, a sealing lid 27 made of a synthetic resin is fitted to the lower end of the first electrode 11, and the first and second electrodes 11,
Spacer 12 made of synthetic resin (insulating material) between lower ends of 12
28, and thus the first and second electrodes 11, 12
Are arranged so that their central axes coincide with each other, and a predetermined gap between them, for example, a gap of about 3 mm, is substantially equally spaced in the longitudinal direction.

【0034】また、第1の電極11の処理済み廃水排出
口14には排出パイプ(排出通路)29の一端が接続さ
れ、排出パイプ29の他端側には廃水を抜く際に用いる
閉鎖弁30が設けられ、閉鎖弁30の上流側からは第2
の排出パイプ31が分岐して設けられ、第2の排出パイ
プ31の途中にはフィルタ32が介設され、第2の排出
パイプ31の他端側は処理済み排水タンク33に至って
いる。
One end of a discharge pipe (discharge passage) 29 is connected to the treated waste water discharge port 14 of the first electrode 11, and the other end of the discharge pipe 29 is a closing valve 30 used for draining waste water. Is provided from the upstream side of the closing valve 30.
Is provided in a branched manner, a filter 32 is provided in the middle of the second discharge pipe 31, and the other end of the second discharge pipe 31 reaches a treated drain tank 33.

【0035】また、第1の電極11には−側の電線34
が接続され、第2の電極12には+側の電線35が接続
されている。なお、第1の電極11の外部に対する絶縁
性を確保できれば、第1の電極11に+、第2の電極1
2に−を、あるいは両電極11、12間に交番電流を通
電するようにしてもよい。
The negative electrode 34 is connected to the first electrode 11.
Are connected, and the + side electric wire 35 is connected to the second electrode 12. If the insulation of the first electrode 11 with respect to the outside can be ensured, the first electrode 11 has + and the second electrode 1 has
Alternatively,-may be applied to 2 or an alternating current may be applied between the electrodes 11 and 12.

【0036】廃水を処理する場合、第1、第2の電極1
1、12間に所定の電流を流す一方、加圧ポンプ24を
作動させる。すると、廃水タンク25内の廃水が所定の
圧力、例えば6kg/cm2に加圧され、廃水導入パイ
プ23、連結ブラケット22及びチタン製パイプ21を
経て第2の電極12に供給される。
When treating wastewater, the first and second electrodes 1
While a predetermined current is passed between 1 and 12, the pressurizing pump 24 is operated. Then, the wastewater in the wastewater tank 25 is pressurized to a predetermined pressure, for example, 6 kg / cm 2 , and supplied to the second electrode 12 via the wastewater introduction pipe 23, the connection bracket 22, and the titanium pipe 21.

【0037】第2の電極12に供給された廃水は第2の
電極12内を流通し、廃水導入口26から第1、第2の
電極11、12間の隙間に流れ込み、第1、第2の電極
11、12の間を流通する。
The wastewater supplied to the second electrode 12 flows through the second electrode 12 and flows from the wastewater inlet 26 into the gap between the first and second electrodes 11 and 12, and the first and second wastewater flows into the gap between the first and second electrodes 11 and 12. Between the electrodes 11 and 12.

【0038】廃水が第1、第2の電極11、12間を流
通する間に廃水には第1、第2の電極11、12から電
気エネルギーが与えられ、廃水中の高分子無機物や高分
子有機物が低分子化され、処理された廃水は処理済み廃
水排出口14から排出パイプ29、フィルタ32及び第
2の排出パイプ31を経て処理済み廃水タンク33に送
られて貯留される。
While the wastewater is flowing between the first and second electrodes 11 and 12, electric energy is given to the wastewater from the first and second electrodes 11 and 12, and high-molecular-weight inorganic substances and polymers in the wastewater are provided. Organic matter is depolymerized, and the treated wastewater is sent from the treated wastewater discharge port 14 to the treated wastewater tank 33 via the discharge pipe 29, the filter 32, and the second discharge pipe 31, and stored therein.

【0039】図2は第2の実施形態を示し、図において
図1と同一符号は同一又は相当部分を示す。本例では廃
水供給パイプ23と排出パイプ29との間に廃水循環パ
イプ(廃水循環通路)36を接続し、廃水循環パイプ3
6の途中に循環ポンプ37を介設している。
FIG. 2 shows a second embodiment, in which the same reference numerals as in FIG. 1 denote the same or corresponding parts. In this example, a wastewater circulation pipe (wastewater circulation passage) 36 is connected between the wastewater supply pipe 23 and the discharge pipe 29, and the wastewater circulation pipe 3
A circulation pump 37 is provided in the middle of 6.

【0040】本例では電解処理済みの廃水の一部が廃水
循環パイプ36及び循環ポンプ37を経て廃水供給パイ
プ23に戻され、第1、第2の電極11、12間におい
て再び処理され、これによって廃水がより確実に処理さ
れることとなる。
In this embodiment, a part of the electrolytically treated wastewater is returned to the wastewater supply pipe 23 via the wastewater circulation pipe 36 and the circulation pump 37, and is treated again between the first and second electrodes 11, 12. As a result, wastewater is more reliably treated.

【0041】図3は第3の実施形態を示す。本例では第
1ないし第nの複数の廃水処理槽10・・・が設けら
れ、第1の廃水処理槽10の廃水流入口38には廃水供
給パイプ23が接続され、第1の廃水処理槽10の処理
済み廃水排出口14には排出パイプ31の一端が接続さ
れ、排出パイプ31の他端側は廃水供給パイプ23とし
て第2の廃水処理槽10の廃水流入口38に接続され、
かかる接続方式が第nの廃水処理槽10まで同様に採用
され、こうして複数の廃水処理槽10・・・をシリアル
に接続した廃水処理槽群が構成されている。
FIG. 3 shows a third embodiment. In this example, a plurality of first to n-th wastewater treatment tanks 10 are provided, a wastewater supply pipe 23 is connected to a wastewater inlet 38 of the first wastewater treatment tank 10, and a first wastewater treatment tank is provided. One end of a discharge pipe 31 is connected to the treated wastewater discharge port 10 of 10, and the other end of the discharge pipe 31 is connected to a wastewater inlet 38 of the second wastewater treatment tank 10 as a wastewater supply pipe 23,
Such a connection method is similarly employed up to the nth wastewater treatment tank 10, and thus a wastewater treatment tank group in which a plurality of wastewater treatment tanks 10 are serially connected is formed.

【0042】このように複数の廃水処理槽10・・・を
直列に接続して廃水を連続的に処理するようにすると、
大量の廃水を効率よく処理できることとなる。
When a plurality of wastewater treatment tanks 10 are connected in series as described above to continuously treat wastewater,
A large amount of wastewater can be treated efficiently.

【0043】図4は第4の実施形態を示し、図において
図1ないし図3と同一符号は同一又は相当部分を示す。
本例では第1の電極11の下端側に廃水流入口38を形
成し、廃水流入口38から入った廃水を第1、第2の電
極11、12間に流通させ、第1の電極11の上端側の
処理済み廃水排出口14から排出させるようになってい
る。
FIG. 4 shows a fourth embodiment, in which the same reference numerals as in FIGS. 1 to 3 denote the same or corresponding parts.
In this example, a wastewater inlet 38 is formed at the lower end side of the first electrode 11, and wastewater that has entered through the wastewater inlet 38 is allowed to flow between the first and second electrodes 11 and 12. The wastewater is discharged from the treated wastewater discharge port 14 on the upper end side.

【0044】なお、第4の実施形態において廃水流入口
38と処理済み廃水排出口14とは逆に配置してもよ
い。
In the fourth embodiment, the wastewater inlet 38 and the treated wastewater outlet 14 may be arranged oppositely.

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

【図1】 本発明に係る廃水処理装置の好ましい実施形
態を示す構成図である。
FIG. 1 is a configuration diagram showing a preferred embodiment of a wastewater treatment apparatus according to the present invention.

【図2】 第2の実施形態を示す構成図である。FIG. 2 is a configuration diagram showing a second embodiment.

【図3】 第3の実施形態を示す構成図である。FIG. 3 is a configuration diagram illustrating a third embodiment.

【図4】 第4の実施形態を示す構成図である。FIG. 4 is a configuration diagram showing a fourth embodiment.

【符号の説明】[Explanation of symbols]

10 廃水処理槽 11 第1の電極 12 第2の電極 14 処理済み廃水排出口 23 廃水供給パイプ(廃水供給通路) 24 加圧ポンプ(加圧手段) 29 排出ポンプ(排出通路) 36 廃水循環パイプ(廃水循環通路) 37 循環ポンプ 38 廃水流入口 Reference Signs List 10 wastewater treatment tank 11 first electrode 12 second electrode 14 treated wastewater outlet 23 wastewater supply pipe (wastewater supply passage) 24 pressurizing pump (pressurizing means) 29 discharge pump (discharge passage) 36 wastewater circulation pipe ( (Wastewater circulation passage) 37 Circulation pump 38 Wastewater inlet

───────────────────────────────────────────────────── フロントページの続き (72)発明者 山下 偉彦 大阪府八尾市服部川6丁目340番地 Fターム(参考) 4D061 DA08 DB19 DC11 DC13 EA03 EA04 EB04 EB14 EB19 EB28 EB30 EB33 FA13  ────────────────────────────────────────────────── ─── Continued on the front page (72) Inventor Yoshihiko Yamashita 6-340 Hattorigawa, Yao-shi, Osaka F-term (reference) 4D061 DA08 DB19 DC11 DC13 DC13 EA03 EA04 EB04 EB14 EB19 EB28 EB30 EB33 FA13

Claims (11)

【特許請求の範囲】[Claims] 【請求項1】 廃水に電気エネルギーを与えて処理を行
う廃水処理装置において、 ほぼ密閉した中空状の第1の電極内に第2の電極を所定
の隙間をあけて収容するとともに該第2の電極を上記第
1の電極に対して絶縁材を介して支持して構成されてな
る廃水処理槽と、 該廃水処理槽の第1、第2の電極の間に電流を通電する
通電手段と、 上記廃水処理槽に設けられ、上記第1の電極と第2の電
極との間に処理すべき廃水を流入させる廃水流入口と、 上記廃水処理槽に設けられ、上記第1の電極と第2の電
極との間で処理された廃水を排出する処理済み廃水排出
口と、 上記廃水流入口に接続された廃水供給通路と、 該廃水供給通路に廃水を加圧して供給する加圧手段と、 上記処理済み廃水排出口に接続された排出通路と、を備
えたことを特徴とする廃水処理装置。
1. A wastewater treatment apparatus for treating wastewater by applying electric energy to a wastewater, wherein a second electrode is accommodated in a substantially closed hollow first electrode with a predetermined gap, and the second electrode is accommodated in the second electrode. A wastewater treatment tank configured to support the electrode with respect to the first electrode via an insulating material, an energizing means for applying an electric current between the first and second electrodes of the wastewater treatment tank, A wastewater inlet provided in the wastewater treatment tank to allow wastewater to be treated to flow between the first electrode and the second electrode; and a first electrode and a second electrode provided in the wastewater treatment tank. A treated wastewater discharge outlet for discharging treated wastewater between the electrodes, a wastewater supply passage connected to the wastewater inlet, and a pressurizing means for pressurizing and supplying wastewater to the wastewater supply passage. And a discharge passage connected to the treated wastewater discharge port. Wastewater treatment device according to.
【請求項2】 上記加圧手段が廃水に対して所定の一定
圧を加圧するようになした請求項1記載の廃水処理装
置。
2. The wastewater treatment apparatus according to claim 1, wherein said pressurizing means pressurizes the wastewater with a predetermined constant pressure.
【請求項3】 上記加圧手段が廃水に対する加圧力を変
動させるようになした請求項1記載の廃水処理装置。
3. The wastewater treatment apparatus according to claim 1, wherein said pressurizing means changes the pressure applied to the wastewater.
【請求項4】 上記廃水処理槽が複数設けられ、該複数
の各廃水処理槽の排出通路に次の廃水処理槽の廃水供給
通路が順次接続されることにより、上記複数の廃水処理
槽が直列に接続された廃水処理槽群を構成している請求
項1記載の廃水処理装置。
4. A plurality of wastewater treatment tanks are provided, and a plurality of wastewater treatment tanks are connected in series by sequentially connecting a wastewater supply passage of a next wastewater treatment tank to a discharge passage of each of the plurality of wastewater treatment tanks. The wastewater treatment apparatus according to claim 1, which constitutes a wastewater treatment tank group connected to the wastewater treatment tank.
【請求項5】 上記廃水供給通路と排出通路との間には
廃水循環通路が接続され、該廃水循環通路には上記排出
通路内の処理済み廃水の一部を上記廃水供給通路に循環
させる循環ポンプが設けられている請求項1又は4記載
の廃水処理装置。
5. A wastewater circulation passage is connected between the wastewater supply passage and the discharge passage, and the wastewater circulation passage circulates a part of the treated wastewater in the discharge passage to the wastewater supply passage. 5. The wastewater treatment device according to claim 1, further comprising a pump.
【請求項6】 長手方向にほぼ均一な内径を有する筒状
をなし、ほぼ密閉構造の第1の電極と、 長手方向にほぼ均一な外径を有する筒状又は棒状をな
し、上記第1の電極内に所定の隙間をあけて収容され、
上記第1の電極に絶縁部材を介して支持された第2の電
極と、 上記第1の電極と第2の電極との間に処理すべき廃水を
流入させる廃水流入口と、 上記第1の電極と第2の電極との間で処理された廃水を
排出する処理済み廃水排出口と、を備えたことを特徴と
する廃水処理槽。
6. A first electrode having a substantially uniform inner diameter in a longitudinal direction and having a substantially hermetically sealed structure, and a first electrode having a substantially uniform outer diameter in a longitudinal direction having a cylindrical or rod shape. It is housed with a predetermined gap in the electrode,
A second electrode supported on the first electrode via an insulating member; a wastewater inlet for flowing wastewater to be treated between the first electrode and the second electrode; A wastewater treatment tank, comprising: a treated wastewater discharge port for discharging treated wastewater between the electrode and the second electrode.
【請求項7】 上記第1の電極が円筒状をなし、上記第
2の電極が円筒状をなし、上記第1、第2の電極が中心
軸線を一致させて配置されている請求項6記載の廃水処
理槽。
7. The device according to claim 6, wherein the first electrode has a cylindrical shape, the second electrode has a cylindrical shape, and the first and second electrodes are arranged with their central axes aligned. Wastewater treatment tank.
【請求項8】 上記第2の電極の一端が開口されて上記
廃水流入口となっている一方、上記第2の電極の他端側
には廃水導入口が形成され、上記第1の電極には上記処
理済み廃水排出口が上記廃水導入口から導入された廃水
を上記第1、第2の電極の間に流通させるように形成さ
れている請求項6又は7記載の廃水処理槽。
8. An end of the second electrode is opened to serve as the wastewater inlet, while a wastewater inlet is formed at the other end of the second electrode. 8. The wastewater treatment tank according to claim 6, wherein the treated wastewater discharge port is formed so that wastewater introduced from the wastewater inlet port flows between the first and second electrodes.
【請求項9】 上記第2の電極の一端が開口されて上記
処理済み廃水排出口となっている一方、上記第2の電極
の他端側には廃水導入口が形成され、上記第1の電極に
は上記廃水流入口が上記第1、第2の電極間を流通した
廃水を上記廃水導入口から第2の電極内に導入させるよ
うに形成されている請求項6又は7記載の廃水処理槽。
9. An end of the second electrode is opened to serve as the treated wastewater discharge port, while a wastewater inlet is formed at the other end of the second electrode. The wastewater treatment according to claim 6 or 7, wherein the wastewater inlet is formed in the electrode so that wastewater flowing between the first and second electrodes is introduced into the second electrode from the wastewater inlet. Tank.
【請求項10】 上記第1の電極が円筒状をなし、上記
第2の電極が断面円形の棒状をなし、上記第1、第2の
電極が中心軸線を一致させて配置されている請求項6記
載の廃水処理槽。
10. The first electrode has a cylindrical shape, the second electrode has a rod shape with a circular cross section, and the first and second electrodes are arranged so that their central axes coincide with each other. 6. The wastewater treatment tank according to 6.
【請求項11】 上記第1の電極の一端側には上記廃水
流入口が、上記第1の電極の他端側には上記処理済み廃
水排出口が各々形成されている請求項6、7又は10の
いずれかに記載の廃水処理槽。
11. The wastewater inflow port is formed at one end of the first electrode, and the treated wastewater discharge port is formed at the other end of the first electrode. A wastewater treatment tank according to any one of Claims 10 to 10.
JP2000118203A 2000-04-19 2000-04-19 Waste water treating device Pending JP2001300536A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP2000118203A JP2001300536A (en) 2000-04-19 2000-04-19 Waste water treating device
KR1020010021258A KR20010098763A (en) 2000-04-19 2001-04-19 A wastewater disposal plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000118203A JP2001300536A (en) 2000-04-19 2000-04-19 Waste water treating device

Publications (1)

Publication Number Publication Date
JP2001300536A true JP2001300536A (en) 2001-10-30

Family

ID=18629389

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (2)

Country Link
JP (1) JP2001300536A (en)
KR (1) KR20010098763A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100448877B1 (en) * 2002-08-19 2004-09-18 한국전력공사 Apparatus for reducing COD from flue-gas desulfurization waste by electrochemical oxidation process

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100457957B1 (en) * 2002-01-11 2004-11-18 김병화 Method for reducing quantity of organic sludge

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10258287A (en) * 1997-03-18 1998-09-29 Sanyo Electric Co Ltd Waste water treatment apparatus
KR100251405B1 (en) * 1997-09-08 2000-04-15 이규철 Wastewater treatment system using electrolysis and photocatalyst and synthetic method of the catalyst
JPH11286796A (en) * 1998-04-06 1999-10-19 Konica Corp Fluidized-bed electrolytic cell, method for recovering and removing metal such as nickel and treatment of water using the cell

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100448877B1 (en) * 2002-08-19 2004-09-18 한국전력공사 Apparatus for reducing COD from flue-gas desulfurization waste by electrochemical oxidation process

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