JPH07284792A - Wastewater treatment method and wastewater treatment equipment - Google Patents
Wastewater treatment method and wastewater treatment equipmentInfo
- Publication number
- JPH07284792A JPH07284792A JP6104676A JP10467694A JPH07284792A JP H07284792 A JPH07284792 A JP H07284792A JP 6104676 A JP6104676 A JP 6104676A JP 10467694 A JP10467694 A JP 10467694A JP H07284792 A JPH07284792 A JP H07284792A
- Authority
- JP
- Japan
- Prior art keywords
- wastewater
- microorganisms
- treatment
- wastewater treatment
- 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.)
- Granted
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Biological Treatment Of Waste Water (AREA)
- Activated Sludge Processes (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
(57)【要約】
【目的】 難分解性物質を効率良く短時間で分解処理で
きる廃水処理方法及び廃水処理装置を提供する。
【構成】 本廃水処理装置は、有機性汚染物質を含有す
る廃水1を微生物2により分解処理する廃水処理装置に
おいて、廃水1を流通させながら微生物2により分解処
理する3つの処理槽3、4、5と、これらの処理槽3、
4、5に配設され且つ廃水1を電気分解して気泡を発生
させる電極棒10及び電極11、12、13と、電極棒
10と電極11、12、13を相対的に回転させる回転
手段とを備え、電極棒10と電極11、12、13間で
廃水1を流れる電流により微生物2を活性化すると共に
気泡18を微生物2をに付着させることを特徴とする。
(57) [Summary] [Purpose] To provide a wastewater treatment method and a wastewater treatment apparatus capable of efficiently decomposing a hardly decomposable substance in a short time. [Structure] This wastewater treatment device is a wastewater treatment device for decomposing wastewater 1 containing organic pollutants with microorganisms 2. In the wastewater treatment device, three treatment tanks 3, 4, for decomposing treatment with microorganisms 2 while circulating the wastewater 1, 5 and these treatment tanks 3,
Electrode rods 10 and electrodes 11, 12 and 13 which are disposed in Nos. 4 and 5 and which electrolyze the waste water 1 to generate bubbles, and rotating means for relatively rotating the electrode rod 10 and the electrodes 11, 12 and 13. It is characterized in that the microorganisms 2 are activated by the electric current flowing through the wastewater 1 between the electrode rod 10 and the electrodes 11, 12, 13 and the bubbles 18 are attached to the microorganisms 2.
Description
【0001】[0001]
【産業上の利用分野】本発明は、難分解性有機物質を分
解できる廃水処理方法及び廃水処理装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a wastewater treatment method and a wastewater treatment apparatus capable of decomposing hardly decomposable organic substances.
【0002】[0002]
【従来の技術】従来の廃水処理装置を用いた廃水処理方
法は、処理槽内に微生物を培養し、この処理槽内へ廃水
を供給し、処理槽内の微生物の作用により廃水中の有機
汚染物質を分解処理するようにしたものである。この方
法では微生物は有機汚染物質を栄養源として増殖し、有
機汚染物質を複数段階で分解して、最終的には二酸化炭
素、エタンなどのガスにまで分解することができる。2. Description of the Related Art A conventional wastewater treatment method using a conventional wastewater treatment apparatus cultivates microorganisms in a treatment tank, supplies the wastewater into the treatment tank, and causes organic contamination in the wastewater by the action of the microorganisms in the treatment tank. It is designed to decompose a substance. According to this method, the microorganisms can grow using organic pollutants as nutrient sources, decompose organic pollutants in multiple stages, and finally decompose them into gases such as carbon dioxide and ethane.
【0003】ところが、科学技術の急激な進展により多
くの有用な化学物質が合成されるに至り、自然界には存
在しない化学物質も多種類合成され、これらの物質は使
用後自然界へ放出されている。自然界から得られる動植
物などの有機物質はそれぞれを廃水として放出しても自
然界に存在する微生物の作用を受けて、あるいはこのよ
うな微生物を利用した廃水処理技術により短時間で分解
処理を行なうことができる。また、合成物質についても
このような微生物により比較的短時間で分解処理するこ
とができるものも多数ある。However, due to rapid progress in science and technology, many useful chemical substances have been synthesized, many kinds of chemical substances which do not exist in nature have been synthesized, and these substances are released to the natural world after use. . Organic substances such as plants and animals obtained from nature can be decomposed in a short time by the action of microorganisms existing in nature even if they are released as wastewater, or by wastewater treatment technology using such microorganisms. it can. Also, many synthetic substances can be decomposed by such microorganisms in a relatively short time.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、合成物
質の中でもメチルナフタレン、イソプロピルアルコー
ル、テトライソプロピルアミンなどのように微生物だけ
では短時間で分解できない、いわゆる難分解性物質の場
合には、微生物を用いた従来の廃水処理方法ではこのよ
うな難分解性物質を短時間で分解処理することが難し
く、微生物は複雑な代謝経路を経た多段階で難分解性物
質を分解をせざるを得ず、その分解処理には例えば18
00時間前後もの長時間を要し、実際には処理不十分の
まま廃水せざるを得ないという課題があった。However, among the synthetic substances, in the case of a so-called hardly decomposable substance such as methylnaphthalene, isopropyl alcohol, tetraisopropylamine, etc., which cannot be decomposed in a short time, the microorganism is used. In the conventional wastewater treatment method, it is difficult to decompose such a persistent substance in a short time, and the microorganism has to decompose the persistent substance in multiple stages through complicated metabolic pathways. For decomposition processing, for example, 18
It took a long time of around 00 hours, and there was a problem that wastewater had to be discharged without treatment.
【0005】本発明は、上記課題を解決するためになさ
れたもので、難分解性物質を効率良く短時間で分解処理
できる廃水処理方法及び廃水処理装置を提供することを
目的としている。The present invention has been made to solve the above problems, and an object of the present invention is to provide a wastewater treatment method and a wastewater treatment apparatus capable of efficiently decomposing a hardly decomposable substance in a short time.
【0006】[0006]
【課題を解決するための手段】本発明者は、難分解性物
質に対する微生物の分解作用について種々研究を重ねた
結果、微生物を特定の環境下に置くと、微生物が活性化
し、従来であれば分解に長時間を要する難分解性物質で
あっても短時間で速やかに分解することが判った。Means for Solving the Problems As a result of various studies on the decomposing action of the microorganism on the hardly decomposable substance, the present inventor has found that when the microorganism is placed in a specific environment, the microorganism is activated, It was found that even a hardly decomposable substance that requires a long time to decompose decomposes quickly in a short time.
【0007】本発明は上記知見に基づいてなされたもの
であり、請求項1に記載の廃水処理方法は、有機性汚染
物質を含有する廃水を微生物により分解処理する廃水処
理方法において、上記廃水内で電流を流すと共に上記廃
水内で磁場を作り、この電流及び磁場により上記廃水中
の微生物を活性化するようにしたものである。The present invention has been made on the basis of the above findings, and the wastewater treatment method according to claim 1 is a wastewater treatment method in which wastewater containing organic pollutants is decomposed by microorganisms. A current is passed through and a magnetic field is created in the wastewater, and the microorganisms in the wastewater are activated by the current and the magnetic field.
【0008】また、本発明の請求項2に記載の廃水処理
方法は、有機性汚染物質を含有する廃水を微生物により
分解処理する廃水処理方法において、上記廃水に電流を
流すと共に上記廃水内で磁場を作り且つ上記廃水内に高
圧空気を断続的に供給して上記廃水中の微生物を活性化
すると共に、上記電流により廃水内で水を電気分解して
気泡を作るようにしたものである。The wastewater treatment method according to claim 2 of the present invention is a wastewater treatment method in which wastewater containing organic pollutants is decomposed by microorganisms, and an electric current is applied to the wastewater and a magnetic field is generated in the wastewater. And intermittently supplying high-pressure air into the wastewater to activate the microorganisms in the wastewater, and at the same time, to electrolyze the water in the wastewater by the electric current to generate bubbles.
【0009】また、本発明の請求項3に記載の廃水処理
装置は、有機性汚染物質を含有する廃水を微生物により
分解処理する廃水処理装置において、上記廃水を流通さ
せながら微生物により分解処理する少なくとも一つの処
理槽と、この処理槽に配設され且つ上記廃水を電気分解
して気泡を発生させる一対の電極と、これら一対の電極
を相対的に回転させる回転手段とを備え、上記一対の電
極間で上記廃水を流れる電流により上記微生物を活性化
すると共に上記気泡を上記微生物に付着させるように構
成されたものである。The wastewater treatment apparatus according to claim 3 of the present invention is a wastewater treatment apparatus for decomposing wastewater containing organic pollutants with microorganisms, and at least decomposing it with microorganisms while circulating the wastewater. The one pair of electrodes is provided with one treatment tank, a pair of electrodes disposed in the treatment tank for electrolyzing the waste water to generate bubbles, and rotating means for relatively rotating the pair of electrodes. It is configured to activate the microorganisms by an electric current flowing through the wastewater between them and to attach the bubbles to the microorganisms.
【0010】また、本発明の請求項4に記載の廃水処理
装置は、請求項3に記載の発明において、上記処理槽
に、上記廃水中に高圧空気を断続的に供給する空気供給
手段を設けたものである。The wastewater treatment apparatus according to a fourth aspect of the present invention is the wastewater treatment apparatus according to the third aspect, wherein the treatment tank is provided with air supply means for intermittently supplying high-pressure air into the wastewater. It is a thing.
【0011】[0011]
【作用】本発明の請求項1に記載の発明によれば、有機
性汚染物質を含有する廃水を微生物により分解処理する
際に、廃水内で電流を流すと共に廃水内で磁場を作る
と、これらの電流及び磁場により微生物が活性化して難
分解性有機物質をも分解処理することがきる。According to the first aspect of the present invention, when a wastewater containing organic pollutants is decomposed by microorganisms, an electric current is passed through the wastewater and a magnetic field is generated in the wastewater. Microorganisms can be activated by the electric current and magnetic field to decompose the persistent organic substances.
【0012】また、本発明の請求項2に記載の発明によ
れば、有機性汚染物質を含有する廃水を微生物により分
解処理する際に、廃水内で電流を流すと共に廃水内で磁
場を作り、更に、廃水内に高圧空気を断続的に供給する
と、電流及び磁場により微生物が活性化すると共に高圧
空気の衝撃波により微生物を刺激してその作用が活発に
なって難分解性物質をも分解処理することができ、更
に、水を電気分解して気泡を発生させると、この気泡が
微生物の周囲に付着して廃水中を浮上し、微生物の散逸
を防止して微生物による分解処理を効率的に行なうこと
ができる。According to the second aspect of the present invention, when the wastewater containing organic pollutants is decomposed by microorganisms, an electric current is passed through the wastewater and a magnetic field is generated in the wastewater. Furthermore, when high-pressure air is intermittently supplied into the wastewater, the microorganisms are activated by the electric current and the magnetic field, and the shock waves of the high-pressure air stimulate the microorganisms to activate their action and decompose the hardly decomposable substances. Further, when water is electrolyzed to generate bubbles, the bubbles adhere to the periphery of the microorganisms and float in the wastewater, preventing the dissipation of the microorganisms and efficiently performing the decomposition treatment by the microorganisms. be able to.
【0013】また、本発明の請求項3に記載の発明によ
れば、廃水処理装置の少なくとの一つの処理槽中で有機
性汚染物質を含有する廃水を流通させながら微生物によ
り分解処理する際に、処理槽内の一対の電極に通電する
と共に回転手段により一対の電極を相対的に回転させる
と、電極間の通電により各電極近傍に磁場が発生し、こ
の磁場が微生物に作用して微生物を活性化する一方、こ
れと同時に各電極表面で酸素などの気泡が発生するが、
各電極は相対的に回転しているため、電極表面の気泡が
微細なまま廃水中に遊離して廃水の流れに抗して気泡が
浮上し、この間に気泡の周囲に微生物が付着して廃水の
流れによる微生物の散逸を防止して微生物による分解処
理を効率的に行なうことができる。According to the third aspect of the present invention, when the waste water containing the organic pollutant is circulated in the at least one treatment tank of the waste water treatment apparatus while being decomposed by microorganisms. In addition, when a pair of electrodes in the treatment tank are energized and the pair of electrodes is relatively rotated by the rotating means, a magnetic field is generated in the vicinity of each electrode due to energization between the electrodes, and the magnetic field acts on the microorganisms to cause the microorganisms to act. Meanwhile, air bubbles such as oxygen are generated on the surface of each electrode at the same time.
Since each electrode rotates relatively, air bubbles on the electrode surface are released into the wastewater while remaining fine, and the air bubbles rise against the flow of the wastewater. It is possible to efficiently dissociate the microorganisms by preventing the microorganisms from being dissipated by the flow of water.
【0014】また、本発明の請求項4に記載の発明によ
れば、請求項3に記載の発明において、上記処理槽に、
上記廃水中に空気を断続的に供給する空気供給手段を設
けたため、廃水内の微生物に空気圧による衝撃波を与え
て微生物を刺激すると共に廃水への酸素の溶解を促進し
て微生物の分解処理を促進することができる。According to the invention described in claim 4 of the present invention, in the invention described in claim 3, the processing tank comprises:
Since the air supply means for intermittently supplying air to the wastewater is provided, a shock wave by air pressure is applied to the microorganisms in the wastewater to stimulate the microorganisms and promote the dissolution of oxygen in the wastewater to promote the decomposition treatment of the microorganisms. can do.
【0015】[0015]
【実施例】以下、図1〜図5に示す実施例に基づいて本
発明を説明する。尚、各図中、図1は本発明の廃水処理
方法に用いられる本発明の廃水処理装置の一実施例を示
す構成図、図2は図1に示す廃水処理装置における微生
物の挙動を説明するための説明図、図3は図1に示す廃
水処理装置の電極を示す斜視図、図4は本発明の廃水処
理方法に用いられる本発明の廃水処理装置の他の実施例
を示す構成図、図5は図4に示す廃水処理装置の要部の
構成を示す構成図である。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below based on the embodiments shown in FIGS. In each figure, FIG. 1 is a configuration diagram showing an embodiment of the wastewater treatment apparatus of the present invention used in the wastewater treatment method of the present invention, and FIG. 2 illustrates the behavior of microorganisms in the wastewater treatment apparatus shown in FIG. 3 is a perspective view showing an electrode of the wastewater treatment apparatus shown in FIG. 1, FIG. 4 is a configuration diagram showing another embodiment of the wastewater treatment apparatus of the present invention used in the wastewater treatment method of the present invention, FIG. 5 is a configuration diagram showing a configuration of a main part of the wastewater treatment device shown in FIG.
【0016】実施例1.本実施例の廃水処理装置は、図
1に示すように、有機性汚染物質を含有する廃水1を微
生物2により分解処理するもので、3つの処理槽3、
4、5が上下方向に3つ積み上げられ、各処理槽が互い
に連結されている。上段の処理槽3の底面3Aは周囲か
ら中心に向かって緩やかに下降傾斜してコーン形状に形
成されており、その中央に開口部が形成されている。ま
た、中段及び下段の処理槽4、5の底面4A、5Aはそ
れぞれ上段の処理槽3と同様に形成され、それぞれの上
面4B、5Bは周囲から中心に向かって緩やかに上昇傾
斜してコーン形状に形成されており、それぞれの中央に
開口部が形成されている。有機汚染物質としては、微生
物2により分解処理され易い物質と、微生物2により分
解処理し難い、メチルナフタレン、イソプロピルアルコ
ール、テトライソプロピルアミンなどの難分解性物質が
ある。また、微生物2としては、好気性のものや嫌気性
のもの、あるいはその中間的なものがあり、本実施例で
は一般的に活性汚泥法に用いられる好気性の微生物を用
いている。Example 1 As shown in FIG. 1, the wastewater treatment apparatus of this example decomposes wastewater 1 containing organic pollutants by microorganisms 2, and three treatment tanks 3,
Three, four and five are stacked vertically, and the processing tanks are connected to each other. The bottom surface 3A of the upper processing tank 3 is formed in a cone shape with a gentle downward slope from the periphery toward the center, and an opening is formed in the center thereof. The bottom surfaces 4A and 5A of the middle and lower processing baths 4 and 5 are formed in the same manner as the upper processing bath 3, respectively, and the upper surfaces 4B and 5B of each of the processing baths 4 and 5 are formed in a cone shape with a gradual upward inclination from the periphery toward the center. And an opening is formed at the center of each of them. Organic pollutants include substances that are easily decomposed by the microorganism 2 and hardly decomposed substances that are difficult to decompose by the microorganism 2, such as methylnaphthalene, isopropyl alcohol, and tetraisopropylamine. The microorganism 2 may be an aerobic microorganism, an anaerobic microorganism, or an intermediate thereof. In this embodiment, an aerobic microorganism generally used in the activated sludge method is used.
【0017】そして、上段の処理槽3と中段の処理槽4
はそれぞれの開口部において筒体6によって連結され、
中段の処理槽4と下段の処理槽5はそれぞれの開口部に
おいて筒体7によって連結され3つの処理槽3、4、5
が一体化している。また、下段の処理槽5の底面5Aの
開口部には筒体8が連結され、この筒体8には上段の処
理槽3の液面まで延びる排出管9が接続されている。こ
れらの処理槽3、4、5及び筒体6、7、8の軸芯はそ
れぞれ一致している。更に、一体化した処理槽3、4、
5内にはそれぞれの軸芯を貫通する磁化された電極棒1
0が配設され、また、各筒体6、7、8の内面には電極
棒10と対をなす筒状の磁化された電極11、12、1
3が取り付けられている。電極棒10と各電極11、1
2、13は、配線14を介して電源15に接続され、こ
の電源15により電極棒10と各電極11、12、13
との間に電圧、例えば5〜40Vの電圧を印加し、処理
槽3、4、5内の廃水1を介して微弱電流、例えば40
〜80mAの電流が流れるようにしてある。更に上記電
極棒10にはモータなどの回転手段(図示せず)が連結
され、この回転手段の駆動により電極棒10が廃水1中
で図1の矢印A方向へ回転するようにしてある。Then, the upper processing tank 3 and the middle processing tank 4
Are connected by a cylinder 6 at each opening,
The middle processing tank 4 and the lower processing tank 5 are connected by a cylindrical body 7 at their respective openings, and three processing tanks 3, 4, 5 are connected.
Are integrated. A cylinder 8 is connected to the opening of the bottom surface 5A of the lower processing tank 5, and a discharge pipe 9 extending to the liquid level of the upper processing tank 3 is connected to the cylindrical body 8. The axes of the processing tanks 3, 4, 5 and the cylindrical bodies 6, 7, 8 are aligned with each other. Furthermore, the integrated processing tanks 3, 4,
A magnetized electrode rod 1 penetrating each shaft core in
0 is arranged, and the cylindrical magnetized electrodes 11, 12, 1 forming a pair with the electrode rod 10 are formed on the inner surfaces of the respective cylinders 6, 7, 8.
3 is attached. Electrode rod 10 and each electrode 11, 1
2 and 13 are connected to a power source 15 via a wiring 14, and the power source 15 causes the electrode rod 10 and each electrode 11, 12, 13 to be connected.
And a voltage of, for example, 5 to 40 V is applied between them and a weak current, for example, 40, through the wastewater 1 in the treatment tanks 3, 4, and 5.
A current of ˜80 mA is allowed to flow. Further, a rotating means (not shown) such as a motor is connected to the electrode rod 10 so that the electrode rod 10 is rotated in the wastewater 1 in the direction of arrow A in FIG.
【0018】また、上段の処理槽3と下段の処理槽5は
配管16により連結され、この配管16を介して処理槽
3と処理槽5が連通している。また、この配管16には
ポンプ17が配設され、このポンプ17の駆動により処
理槽3に供給された廃水1が処理槽4、5を経由して配
管16から元の処理槽3へ循環するようにしてある。そ
して、廃水1が処理槽3、4、5を繰り返し循環する間
に微生物2が廃水1中の有機汚染物質に作用して分解処
理し、最終的には二酸化炭素、メタン等のガスまで分解
して廃水1を浄化し、浄化された処理水は排出管9を介
して排水するようになっている。排水後には処理槽3へ
廃水1を自動的に補給し、廃水1が常に一定量を確保す
るようにしてある。The upper processing bath 3 and the lower processing bath 5 are connected by a pipe 16, and the processing bath 3 and the processing bath 5 are connected to each other through the pipe 16. Further, a pump 17 is arranged in the pipe 16, and the waste water 1 supplied to the treatment tank 3 by driving the pump 17 circulates from the pipe 16 to the original treatment tank 3 via the treatment tanks 4 and 5. Is done. Then, while the wastewater 1 is repeatedly circulated in the treatment tanks 3, 4, and 5, the microorganisms 2 act on the organic pollutants in the wastewater 1 to decompose it, and finally decompose into gases such as carbon dioxide and methane. The wastewater 1 is purified by means of the wastewater 1, and the purified treated water is discharged through the discharge pipe 9. After the drainage, the waste water 1 is automatically replenished to the treatment tank 3 so that the waste water 1 always maintains a constant amount.
【0019】次に、上記実施例の廃水処理装置を用いた
本発明の廃水処理方法の一実施例を上記廃水処理装置の
動作と共に説明する。まず、廃水1を処理槽3、4、5
内へ供給し、各処理槽3、4、5内で微生物2を廃水1
により混濁状態にする。そして、廃水1のpHを予め7
〜9.5に調整しておき、電極棒10を回転手段により
回転させながら電源15から電極棒10と電極11、1
2、13間に30Vの電圧を印加して電極間に40〜8
0mAの微弱電流を流す。これと同時にポンプ17を駆
動して処理槽3、4、5内の廃水1を配管15を介して
緩やかに循環させ、各処理槽3、4、5内で廃水1の下
降流を作る。これにより微生物2は図2の矢印Bで示す
ように各処理槽3、4、5の下方へ流れるが、その多く
は後述のように気泡18と共に上昇する。Next, an embodiment of the wastewater treatment method of the present invention using the wastewater treatment equipment of the above embodiment will be explained together with the operation of the wastewater treatment equipment. First, the wastewater 1 is treated with the treatment tanks 3, 4, 5
Supplied to the inside, and the microorganisms 2 in each treatment tank 3, 4, 5 waste water 1
To make it cloudy. Then, the pH of the wastewater 1 is set to 7 in advance.
Adjusted to 9.5, and the electrode rod 10 and the electrodes 11 and 1 from the power source 15 while rotating the electrode rod 10 by the rotating means.
A voltage of 30 V is applied between the electrodes 2 and 13 and the voltage is 40 to 8 between the electrodes.
A weak current of 0 mA is applied. At the same time, the pump 17 is driven to gently circulate the wastewater 1 in the treatment tanks 3, 4, and 5 through the pipe 15 to create a downward flow of the wastewater 1 in each treatment tank 3, 4, and 5. As a result, the microorganisms 2 flow under the treatment tanks 3, 4, 5 as shown by the arrow B in FIG. 2, but most of them rise with the bubbles 18 as described later.
【0020】即ち、上述の電流により+側の電極棒10
では酸素ガスが生成し、−側の電極11、12、13で
は水素ガスが生成する。各電極ではそれぞれのガスが徐
々に成長して気泡18になるが、この時電極棒10が回
転しているため、電極棒10に付着した気泡18は電極
棒10の回転により微細な状態で電極棒10から遊離し
て廃水1内を浮上し、微生物2の表面に付着する。微生
物2への気泡18の付着量が多くなると微生物2に浮力
が作用して微生物2が廃水1中をその下降流に抗して図
2の矢印Cで示すように上昇する。そのため、処理槽
3、4、5内では廃水1が循環する間でも、気泡18が
微生物2の下流側への流れを抑制すると共に各処理槽
3、4、5内へ逆流させて微生物2を濃縮し、有機汚染
物質の分解処理に対して微生物2を効率良く使うことが
できる。また、各処理槽3、4、5から微生物2が下流
側へ流れても、配管9を介して各処理槽3、4、5へ微
生物2を戻すことができる。That is, the above-mentioned current causes the positive electrode rod 10 to move.
Oxygen gas is generated at, and hydrogen gas is generated at the-side electrodes 11, 12, and 13. At each electrode, each gas gradually grows and becomes a bubble 18. At this time, since the electrode rod 10 is rotating, the bubble 18 adhering to the electrode rod 10 is finely divided by the rotation of the electrode rod 10 into an electrode. It is released from the rod 10 and floats in the wastewater 1 and adheres to the surface of the microorganism 2. When the amount of bubbles 18 attached to the microorganisms 2 increases, buoyancy acts on the microorganisms 2 and the microorganisms 2 rise in the wastewater 1 against the downward flow thereof as shown by an arrow C in FIG. Therefore, even while the wastewater 1 circulates in the treatment tanks 3, 4, and 5, the bubbles 18 suppress the flow of the microorganisms 2 to the downstream side and make the microorganisms 2 flow back into the respective treatment tanks 3, 4, and 5 to cause the microorganisms 2 to flow. The microorganism 2 can be efficiently used for concentration and decomposition treatment of organic pollutants. Further, even if the microorganisms 2 flow from the respective treatment tanks 3, 4, 5 to the downstream side, the microorganisms 2 can be returned to the respective treatment tanks 3, 4, 5 via the pipe 9.
【0021】一方、処理中には磁化された電極棒10と
磁化された各電極11、12、13間に電圧を印加して
いるため、各電極の周囲には磁場が形成され、この磁場
が電極間を流れる電流と共に微生物2に作用して微生物
2を活性化し、分解し易い有機汚染物質を選択的に分解
するという、微生物2の選択性を抑制し、微生物2に対
して難分解性物質をも分解する特性を付与し、このよう
な難分解性物質の分解に強い微生物2として馴化培養し
て微生物2の難分解性物質に対する活性を増強すること
ができる。これは電流及び磁場の作用により微生物2が
刺激され、その呼吸性及び代謝性が活発になったために
起きる現象と考えられる。そして、この現象及び馴化培
養により微生物2の細胞内と細胞外との間で物質の輸送
機能が高まり、難分解性物質をそれ以外の有機汚染物質
に匹敵する速度で栄養源として細胞内に取り込み、難分
解性物質を短時間で速やかに分解処理することができ
る。そして、このように活性化した微生物2が気泡18
の作用を受けて各処理槽3、4、5内へ浮上し、各処理
槽3、4、5内では気泡18からの溶解酸素と相俟って
微生物2は分解し易い有機汚染物質を分解処理すると共
に、難分解性物質をも他の分解し易い有機汚染物質と同
様に短時間で分解処理することができ、化学的酸素要求
量がCOD=30の廃水1であって本実施例における微
生物2により分解処理することができる。この際の難分
解性物質の分解除去率は99%に達し、従来の処理方法
が20%前後であることと比較すると本実施例における
分解除去率は格段に向上する。また、有機汚染物質の消
化と相俟って酸素ガスの溶解により微生物2が繁殖す
る。ここで、微生物2による難分解性物質の分解処理能
力を更に高める場合には、微生物2を担体に付着させる
ことによりその目的を達成することができる。On the other hand, during the processing, since a voltage is applied between the magnetized electrode rod 10 and the magnetized electrodes 11, 12 and 13, a magnetic field is formed around each electrode, and this magnetic field is generated. With the current flowing between the electrodes, it acts on the microorganisms 2 to activate the microorganisms 2, selectively decomposing organic pollutants that are easily decomposed, which suppresses the selectivity of the microorganisms 2 and is a substance that is difficult to decompose with respect to the microorganisms 2. It is possible to enhance the activity of the microorganism 2 against the hardly-decomposable substance by imparting the property of decomposing the same to the microorganism 2 and acclimatizing and culturing the microorganism 2 as a microorganism 2 having a strong resistance to the decomposition of the hardly-decomposable substance. This is considered to be a phenomenon that occurs because the microorganisms 2 are stimulated by the action of an electric current and a magnetic field and their respiratory and metabolic properties are activated. Then, due to this phenomenon and conditioned culture, the transport function of the substance between the inside and outside of the cell of the microorganism 2 is enhanced, and the hardly decomposable substance is taken into the cell as a nutrient source at a speed comparable to that of other organic pollutants. Therefore, the hardly decomposable substance can be decomposed rapidly in a short time. Then, the microorganisms 2 activated in this way generate bubbles 18
Is floated up into the respective treatment tanks 3, 4, and 5, and in the respective treatment tanks 3, 4, and 5, the microorganism 2 is decomposed in combination with the dissolved oxygen from the bubbles 18 to be easily decomposed. In addition to processing, hardly decomposable substances can be decomposed in a short time like other organic pollutants which are easily decomposed, and the waste water 1 having a chemical oxygen demand of COD = 30 is used in the present embodiment. It can be decomposed by the microorganism 2. At this time, the decomposition and removal rate of the hardly decomposable substance reaches 99%, and the decomposition and removal rate in this example is remarkably improved as compared with the conventional treatment method of about 20%. In addition to the digestion of organic pollutants, the microorganisms 2 propagate due to the dissolution of oxygen gas. Here, in the case of further enhancing the decomposition treatment capability of the hardly decomposable substance by the microorganism 2, the purpose can be achieved by attaching the microorganism 2 to the carrier.
【0022】以上説明したように上記実施例装置を用い
た本実施例の廃水処理方法によれば、各処理槽3、4、
5の電極11、12、13と電極棒10間に電圧を印加
し、電極棒10と各電極11、12、13間で電流を流
し、しかも各電極近傍の廃水1内で磁場を作ると、この
電流及び磁場により廃水1中の微生物2を活性化するこ
とにより、微生物2の細胞内と細胞外との間で物質の輸
送機能が高まり、難分解性物質をそれ以外の有機汚染物
質に匹敵する速度で細胞内に取り込み、難分解性物質を
短時間で速やかに分解処理することができ、難分解性物
質の分解除去率が99%に達する。従って、従来の処理
装置を用いた廃水処理方法の難分解性物質の分解除去率
が20%前後であることと比較すると本実施例ではその
分解除去率が格段に向上する。そのため本実施例によれ
ば、廃水処理装置の設置容積を格段に削減することがで
き、その設置面積を例えば従来の設置容積の1/10以
下にすることができる。As described above, according to the wastewater treatment method of this embodiment using the apparatus of the above embodiment, the treatment tanks 3, 4,
When a voltage is applied between the electrodes 11, 12, 13 and the electrode rod 10 of No. 5, an electric current is passed between the electrode rod 10 and each of the electrodes 11, 12, 13 and a magnetic field is created in the wastewater 1 near each electrode, By activating the microorganisms 2 in the wastewater 1 by this electric current and magnetic field, the transport function of substances between the inside and outside of the cells of the microorganisms 2 is enhanced, and persistent substances are comparable to other organic pollutants. It can be taken up into cells at a rate that can be rapidly decomposed in a short time, and the decomposition and removal rate of the hardly decomposed substance reaches 99%. Therefore, in comparison with the decomposition and removal rate of the hardly decomposable substance in the wastewater treatment method using the conventional processing apparatus being around 20%, the decomposition and removal rate is remarkably improved in this embodiment. Therefore, according to the present embodiment, the installation volume of the wastewater treatment device can be significantly reduced, and the installation area can be reduced to, for example, 1/10 or less of the conventional installation volume.
【0023】実施例2.本実施例の廃水処理装置20
は、図4に示すように、廃水1を貯留する貯留槽21の
側壁に配管22を介して接続されている。この配管22
の上流側にはポンプ23が配設され、このポンプにより
廃水処理装置20と貯留槽21との間を廃水1が循環
し、この間に廃水処理装置20の微生物2により有機汚
染物質を分解処理するように構成されている。この貯留
槽21には廃水処理装置20が取り付けられた側壁とは
別の位置に排出管24が取り付けられ、廃水処理装置2
0による処理水を排出管24から排水するようにしてい
る。Embodiment 2. Wastewater treatment apparatus 20 of this embodiment
Is connected to the side wall of a storage tank 21 that stores the wastewater 1 via a pipe 22 as shown in FIG. This piping 22
A pump 23 is disposed on the upstream side of the waste water 1, and the waste water 1 circulates between the waste water treatment device 20 and the storage tank 21 by this pump, and during this period, the organic pollutants are decomposed by the microorganisms 2 of the waste water treatment device 20. Is configured. A discharge pipe 24 is attached to the storage tank 21 at a position different from the side wall on which the wastewater treatment device 20 is attached.
The treated water of 0 is discharged from the discharge pipe 24.
【0024】そこで、本実施例の廃水処理装置20を図
5を参照しながら詳述する。本実施例の廃水処理装置2
0は、図5に示すように、横長で筒状の処理槽201、
202が上下方向に2つ積み上げられて構成されてい
る。下段の処理槽201の左右両側にはそれぞれ上下逆
方向に向く配管部201A、201Bが形成され、ま
た、上段の処理槽202の左右両側にも同様に上下を向
く配管部202A、202Bが形成されている。そし
て、上下の処理槽201、202はそれぞれの配管部2
01A、202Bにおいて接続配管を兼ねる電極203
を介してそれぞれのフランジにより連結されている。ま
た、下段の処理槽201両端には蓋201C、201C
がボルトなどにより接合され、これらの蓋201C、2
01Cにより処理槽201内を封止してある。Therefore, the wastewater treatment apparatus 20 of this embodiment will be described in detail with reference to FIG. Wastewater treatment apparatus 2 of this embodiment
As shown in FIG. 5, 0 is a horizontally long cylindrical processing tank 201,
Two 202 are stacked vertically. Piping portions 201A and 201B that face up and down are formed on the left and right sides of the lower processing tank 201, and pipe portions 202A and 202B that vertically face are formed on the left and right sides of the upper processing tank 202, respectively. ing. The upper and lower processing tanks 201 and 202 are respectively connected to the pipe section 2
Electrodes 203 also serving as connection pipes in 01A and 202B
Are connected by respective flanges. Further, the lids 201C and 201C are provided at both ends of the lower processing tank 201.
Are joined by bolts or the like, and these lids 201C, 2
The inside of the processing tank 201 is sealed by 01C.
【0025】また、処理槽201には蓋201C、20
1Cの中心を電極棒204がシール部材205を介して
貫通しており、しかもこの電極棒204は図示しない回
転手段により回転可能に構成されている。この処理槽2
01の外周及び電極棒204の両端部の外周はコイル2
06A、206Bにより隙間を介して囲まれており、こ
れらのコイル206A、206Bは互いに配線207に
より接続されて一体化している。一方のコイル206B
の一端は電源の−側に接続され、他方のコイル206B
の一端は電極棒204の左端に接続されている。また、
電源の+側は処理槽201、202間の電極203に接
続され、処理槽201内の廃水1を介して電極棒204
との間で微弱電流が流れ、この電流によりコイル206
A、206Bの内側即ち処理槽201内に磁場が形成さ
れるように構成されている。また、上段の処理槽202
も電極棒208、シール部材209、コイル210A、
210B及び配線211を有し、上記処理槽201と同
様に構成されている。The processing tank 201 has lids 201C and 20C.
The electrode rod 204 penetrates through the center of 1C via a seal member 205, and the electrode rod 204 is configured to be rotatable by a rotating means (not shown). This processing tank 2
The outer circumference of 01 and the outer circumference of both ends of the electrode rod 204 are coil 2
The coils 206A and 206B are surrounded by the gaps 06A and 206B, and the coils 206A and 206B are connected to each other by a wiring 207 to be integrated. One coil 206B
Is connected to the negative side of the power supply, and the other coil 206B
Is connected to the left end of the electrode rod 204. Also,
The + side of the power source is connected to the electrode 203 between the treatment tanks 201 and 202, and the electrode rod 204 is connected via the waste water 1 in the treatment tank 201.
A weak current flows between the coil 206 and
A magnetic field is formed inside the A and 206B, that is, inside the processing tank 201. In addition, the upper processing tank 202
Also the electrode rod 208, the seal member 209, the coil 210A,
It has 210B and wiring 211, and is configured similarly to the processing tank 201.
【0026】更に、電極棒204には右端から処理槽2
01内に至る空気通路204Aが軸芯を通るように形成
され、この空気通路204Aは軸芯に直交する方向に向
けて処理槽201内で開口している。この空気通路20
4Aの軸端の開口には空気配管212が気密を保って接
続されている。この空気配管212には高圧空気源(図
示せず)が接続され、更に、この空気配管212には電
磁バルブ213及びバルブ214が下流側から上流側へ
順次配設され、バルブ214の開度を調整した状態で電
磁バルブ213を断続的に開放することにより高圧空気
源の高圧空気を処理槽201内の廃水1中へ断続的に供
給し、廃水1中の微生物(図示せず)に空気の衝撃波を
付与するように構成されている。尚、図示してないが処
理槽202の電極棒208にも同様の空気通路が施さ
れ、高圧空気の衝撃波を処理槽202内の微生物に付与
できるようになっている。Further, the processing bath 2 is attached to the electrode rod 204 from the right end.
An air passage 204A reaching 01 is formed so as to pass through the axis, and the air passage 204A opens in the processing tank 201 in a direction orthogonal to the axis. This air passage 20
An air pipe 212 is airtightly connected to the opening at the shaft end of 4A. A high-pressure air source (not shown) is connected to the air pipe 212, and an electromagnetic valve 213 and a valve 214 are sequentially arranged in the air pipe 212 from the downstream side to the upstream side, and the opening degree of the valve 214 is adjusted. In the adjusted state, the electromagnetic valve 213 is intermittently opened to intermittently supply the high-pressure air from the high-pressure air source into the wastewater 1 in the treatment tank 201, and the microorganisms (not shown) in the wastewater 1 are supplied with air. It is configured to impart a shock wave. Although not shown, the electrode rod 208 of the treatment tank 202 is also provided with a similar air passage so that a shock wave of high-pressure air can be applied to the microorganisms in the treatment tank 202.
【0027】次に、上記実施例の廃水処理装置を用いた
本発明の廃水処理方法の一実施例を上記廃水処理装置の
動作と共に説明する。まず、廃水1を処理槽201内へ
供給し、各処理槽201、202内で微生物を廃水1に
より混濁状態にする。そして、廃水1のpHを予め7〜
9.5に調整しておき、電極棒204を回転手段により
回転させながら電源から例えば5〜40Vの電圧を電極
203及びコイル206A、206Bへ印加すると、こ
の電圧は結局、電極棒204と電極203との間に印加
されることになる。これにより電極203と電極棒20
4間の電圧により廃水1を介して40〜80mAの微弱
電流が流れる。この時ポンプ23が駆動していると、貯
留槽21内の廃水1が貯留槽21と処理槽201、20
2との間で循環し、廃水1は処理槽201から処理槽2
02への緩やかな上昇流を作る。この際処理槽202に
ついても処理槽201と同様の現象が起こる。Next, one embodiment of the wastewater treatment method of the present invention using the wastewater treatment apparatus of the above embodiment will be described together with the operation of the wastewater treatment apparatus. First, the wastewater 1 is supplied into the treatment tank 201, and the microorganisms are made turbid by the wastewater 1 in the respective treatment tanks 201 and 202. Then, the pH of the wastewater 1 is set to 7-
When the voltage is adjusted to 9.5 and a voltage of, for example, 5 to 40 V is applied from the power supply to the electrode 203 and the coils 206A and 206B while rotating the electrode rod 204 by the rotating means, this voltage eventually results in the electrode rod 204 and the electrode 203. Will be applied between. Thereby, the electrode 203 and the electrode rod 20
The voltage between 4 causes a weak current of 40 to 80 mA to flow through the wastewater 1. At this time, when the pump 23 is driven, the wastewater 1 in the storage tank 21 is stored in the storage tank 21 and the processing tanks 201, 20.
2 and the wastewater 1 is circulated from the treatment tank 201 to the treatment tank 2
Make a gentle updraft to 02. At this time, the same phenomenon occurs in the processing bath 202 as in the processing bath 201.
【0028】一方、コイル206A、206B、210
A、210Bを流れる電流により処理槽201、202
内で磁場を作り、この磁場と廃水1内での微弱電流とが
相俟って実施例1の場合と同様に処理槽201、202
内の微生物を活性化して廃水1内の難分解性物質を含む
有機汚染物質を実施例1の場合と同様に分解処理する。
この時、電磁バルブ213を断続的に開閉して開度調整
されたバルブ214、空気配管212及び空気通路20
4Aを介して高圧空気を処理槽201内へ断続的に供給
すると、この空気は空気通路204Aから処理槽201
内へ空気の衝撃波を与えて微生物を活性化してその代謝
機能を増進すると共に酸素を廃水1内へ溶解することが
できる。On the other hand, the coils 206A, 206B, 210
Processing tanks 201 and 202 by the electric current flowing through A and 210B
A magnetic field is generated in the treatment tank 201, 202, as in the case of the first embodiment, because the magnetic field and the weak current in the wastewater 1 are combined.
The microorganisms therein are activated and the organic pollutants containing the hardly decomposable substance in the wastewater 1 are decomposed in the same manner as in Example 1.
At this time, the electromagnetic valve 213 is intermittently opened and closed to adjust the opening degree of the valve 214, the air pipe 212, and the air passage 20.
When high-pressure air is intermittently supplied into the processing tank 201 via 4A, this air is supplied from the air passage 204A to the processing tank 201.
A shock wave of air can be applied inside to activate microorganisms to enhance their metabolic function and oxygen can be dissolved in the wastewater 1.
【0029】以上説明したように上記実施例装置を用い
た本実施例の廃水処理方法によれば、各電極棒204、
208と電極203と間に電圧を印加し、電極棒20
4、208と電極203間で電流を流し、しかも各処理
槽201、202の廃水1内で磁場を作ると、この電流
及び磁場により廃水1中の微生物を活性化し、更に高圧
空気の断続的な衝撃波により微生物が活性化し、微生物
の細胞内と細胞外との間で物質の輸送機能(代謝機能)
が高まり、難分解性物質をそれ以外の有機汚染物質に匹
敵する速度で細胞内に取り込み、難分解性物質を短時間
で速やかに分解処理することができる。その他、本実施
例においても実施例1と同様の作用効果を期することが
できる。As described above, according to the wastewater treatment method of this embodiment using the apparatus of the above embodiment, each electrode rod 204,
A voltage is applied between the electrode 208 and the electrode 203, and the electrode rod 20
When a current is passed between the electrodes 4, 208 and the electrode 203 and a magnetic field is created in the wastewater 1 of each treatment tank 201, 202, the microorganisms in the wastewater 1 are activated by the current and the magnetic field, and the high-pressure air is intermittently supplied. The shock wave activates the microorganism, and transports substances (metabolic function) between the inside and outside of the microorganism.
Therefore, the hardly decomposable substance can be taken into cells at a rate comparable to other organic pollutants, and the hardly decomposable substance can be rapidly decomposed in a short time. In addition, also in the present embodiment, the same operational effect as that of the first embodiment can be expected.
【0030】尚、本発明は上記各実施例に何等制限され
るものではなく、廃水内の微生物を電流及び磁場により
活性化するという本発明の要旨内に包含される技術であ
れば、本発明の各構成要素を適宜設計変更したものであ
っても本発明に包含される。It should be noted that the present invention is not limited to the above-mentioned embodiments at all, and any technique included in the gist of the present invention of activating microorganisms in wastewater by an electric current and a magnetic field can be applied to the present invention. The present invention includes even those in which the respective components of (1) are appropriately designed and changed.
【0031】[0031]
【発明の効果】本発明の請求項1及び請求項2に記載の
発明によれば、難分解性物質を効率良く短時間で分解処
理できる廃水処理方法及び廃水処理装置を提供すること
がきる。According to the first and second aspects of the present invention, it is possible to provide a wastewater treatment method and a wastewater treatment apparatus capable of efficiently decomposing a hardly decomposable substance in a short time.
【0032】また、本発明の請求項3及び請求項4に記
載の発明によれば、難分解性物質を効率良く短時間で分
解処理できる廃水処理装置を提供することがきる。According to the third and fourth aspects of the present invention, it is possible to provide a wastewater treatment apparatus capable of efficiently decomposing a hardly decomposable substance in a short time.
【図1】本発明の廃水処理方法に用いられる本発明の廃
水処理装置の一実施例を示す構成図である。FIG. 1 is a configuration diagram showing an embodiment of a wastewater treatment apparatus of the present invention used in a wastewater treatment method of the present invention.
【図2】図1に示す廃水処理装置における微生物の挙動
を説明するための説明図である。FIG. 2 is an explanatory diagram for explaining the behavior of microorganisms in the wastewater treatment device shown in FIG.
【図3】図1に示す廃水処理装置の電極を示す斜視図で
ある。3 is a perspective view showing electrodes of the wastewater treatment device shown in FIG. 1. FIG.
【図4】本発明の廃水処理方法に用いられる本発明の廃
水処理装置の他の実施例を示す構成図である。FIG. 4 is a configuration diagram showing another embodiment of the wastewater treatment apparatus of the present invention used in the wastewater treatment method of the present invention.
【図5】図4に示す廃水処理装置の要部の構成を示す構
成図である。5 is a configuration diagram showing a configuration of a main part of the wastewater treatment device shown in FIG.
1 廃水 2 微生物 3 処理槽 4 処理槽 5 処理槽 10 電極棒 11 電極 12 電極 13 電極 18 気泡 20 廃水処理装置 201 処理槽 202 処理槽 203 電極 204 電極棒 206A コイル 206B コイル 210A コイル 210B コイル 1 Wastewater 2 Microorganisms 3 Treatment tank 4 Treatment tank 5 Treatment tank 10 Electrode rod 11 Electrode 12 Electrode 13 Electrode 18 Bubble 20 Wastewater treatment device 201 Treatment tank 202 Treatment tank 203 Electrode 204 Electrode 206A coil 206B coil 210A coil 210B coil
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 3/12 ZAB E ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location C02F 3/12 ZAB E
Claims (4)
により分解処理する廃水処理方法において、上記廃水内
で電流を流すと共に上記廃水内で磁場を作り、この電流
及び磁場により上記廃水中の微生物を活性化することを
特徴とする廃水処理方法。1. In a wastewater treatment method for decomposing wastewater containing organic pollutants by microorganisms, an electric current is passed through the wastewater and a magnetic field is generated within the wastewater, and the microorganisms in the wastewater are generated by the electric current and the magnetic field. A method for treating wastewater, which comprises activating water.
により分解処理する廃水処理方法において、上記廃水に
電流を流すと共に上記廃水内で磁場を作り且つ上記廃水
内に高圧空気を断続的に供給して上記廃水中の微生物を
活性化すると共に、上記電流により廃水内で水を電気分
解して気泡を作ることを特徴とする廃水処理方法。2. A wastewater treatment method for decomposing wastewater containing organic pollutants by microorganisms, wherein an electric current is applied to the wastewater, a magnetic field is created in the wastewater, and high-pressure air is intermittently supplied into the wastewater. And activating the microorganisms in the wastewater, and at the same time, electrolyzing the water in the wastewater by the electric current to form bubbles.
により分解処理する廃水処理装置において、上記廃水を
流通させながら微生物により分解処理する少なくとも一
つの処理槽と、この処理槽に配設され且つ上記廃水を電
気分解して気泡を発生させる一対の電極と、これら一対
の電極を相対的に回転させる回転手段とを備え、上記一
対の電極間で上記廃水を流れる電流により上記微生物を
活性化すると共に上記気泡を上記微生物に付着させるこ
とを特徴とする廃水処理装置。3. A wastewater treatment apparatus for decomposing wastewater containing organic pollutants with microorganisms, at least one treatment tank for decomposing treatment with microorganisms while circulating the wastewater, and disposed in this treatment tank. A pair of electrodes for electrolyzing the waste water to generate bubbles and a rotating means for relatively rotating the pair of electrodes are provided, and the microorganisms are activated by an electric current flowing through the waste water between the pair of electrodes. A wastewater treatment apparatus, characterized in that the bubbles are attached to the microorganisms.
断続的に供給する空気供給手段を設けたことを特徴とす
る請求項3に記載の廃水処理装置。4. The wastewater treatment apparatus according to claim 3, wherein the treatment tank is provided with air supply means for intermittently supplying high-pressure air into the wastewater.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10467694A JP3244154B2 (en) | 1994-04-19 | 1994-04-19 | Wastewater treatment method and wastewater treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10467694A JP3244154B2 (en) | 1994-04-19 | 1994-04-19 | Wastewater treatment method and wastewater treatment device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH07284792A true JPH07284792A (en) | 1995-10-31 |
| JP3244154B2 JP3244154B2 (en) | 2002-01-07 |
Family
ID=14387079
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10467694A Expired - Fee Related JP3244154B2 (en) | 1994-04-19 | 1994-04-19 | Wastewater treatment method and wastewater treatment device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3244154B2 (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0861887A3 (en) * | 1997-02-18 | 1999-08-04 | Canon Kabushiki Kaisha | Microbial processes using electrolyzed water |
| WO2004096718A1 (en) * | 2003-05-02 | 2004-11-11 | Daiei Corporation | Purification system |
| JP2008119674A (en) * | 2006-11-10 | 2008-05-29 | Aw Engineering Ltd | Electrolysis activated sludge treatment method and its apparatus |
| JP2009078244A (en) * | 2007-09-27 | 2009-04-16 | Sharp Corp | Exhaust gas treatment device and exhaust gas treatment method |
| JP2020025952A (en) * | 2018-08-17 | 2020-02-20 | 田村 善胤 | Water purification equipment |
| KR102443730B1 (en) * | 2021-08-21 | 2022-09-15 | (주)지티앤 | Rotary electrode type electrolysis device |
| KR20240036291A (en) * | 2022-09-13 | 2024-03-20 | (주)지티앤 | Continual system for processing waste water |
-
1994
- 1994-04-19 JP JP10467694A patent/JP3244154B2/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0861887A3 (en) * | 1997-02-18 | 1999-08-04 | Canon Kabushiki Kaisha | Microbial processes using electrolyzed water |
| WO2004096718A1 (en) * | 2003-05-02 | 2004-11-11 | Daiei Corporation | Purification system |
| JP2008119674A (en) * | 2006-11-10 | 2008-05-29 | Aw Engineering Ltd | Electrolysis activated sludge treatment method and its apparatus |
| JP2009078244A (en) * | 2007-09-27 | 2009-04-16 | Sharp Corp | Exhaust gas treatment device and exhaust gas treatment method |
| JP2020025952A (en) * | 2018-08-17 | 2020-02-20 | 田村 善胤 | Water purification equipment |
| KR102443730B1 (en) * | 2021-08-21 | 2022-09-15 | (주)지티앤 | Rotary electrode type electrolysis device |
| KR20240036291A (en) * | 2022-09-13 | 2024-03-20 | (주)지티앤 | Continual system for processing waste water |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3244154B2 (en) | 2002-01-07 |
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