JP2000033379A - Electrolytic sterilizer - Google Patents

Electrolytic sterilizer

Info

Publication number
JP2000033379A
JP2000033379A JP10202280A JP20228098A JP2000033379A JP 2000033379 A JP2000033379 A JP 2000033379A JP 10202280 A JP10202280 A JP 10202280A JP 20228098 A JP20228098 A JP 20228098A JP 2000033379 A JP2000033379 A JP 2000033379A
Authority
JP
Japan
Prior art keywords
water
treated
electrode
anode electrode
electrolytic
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
JP10202280A
Other languages
Japanese (ja)
Inventor
Yasuto Kondo
康人 近藤
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP10202280A priority Critical patent/JP2000033379A/en
Publication of JP2000033379A publication Critical patent/JP2000033379A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide an electrolytic sterilizer sterilizing the microorganisms contained in the water to be treated by furnishing a fibrous activated carbon and a porous metal to the electrodes arranged in an electrolytic cell. SOLUTION: The water to be treated is passed through an electrolytic cell 1 in which an anode is opposed to a cathode to sterilize the microorganisms such as bacteria and protozoa by this electrolytic sterilizer 3. A cylindrical fibrous activated carbon 4 is provided to the anode and a reticular or porous metal 5 to the cathode, and the anode is disposed within the cathode.

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】この発明は、被処理水中に含
まれている細菌や原生動物等の微生物の殺菌を行う電解
殺菌装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrolytic sterilizer for sterilizing microorganisms such as bacteria and protozoa contained in water to be treated.

【0002】[0002]

【従来の技術】被処理水を殺菌できる技術として、電解
殺菌の方式が紹介され、予想されるメリットが大きいた
め、実用化が期待されている。この方式の殺菌のメカニ
ズムは、細菌や原生動物等の微生物の生細胞が電極(陽
極)に接触すると、細胞と電極間で電子移動反応が生
じ、細胞内補酵素の酸化還元反応が起こり、当該細胞の
活性が低下するという事で知られている。しかし単に陽
極に微生物の細胞を接触させると言っても、被処理水の
中に散在する微生物のすべてを陽極に接触させることは
困難で、利用すべき技術が見当たらない状況にあったか
ら、実用化が遅れている。
2. Description of the Related Art As a technique capable of sterilizing water to be treated, an electrolytic sterilization method is introduced, and its expected merits are great, and its practical application is expected. The mechanism of sterilization in this method is that when live cells of microorganisms such as bacteria and protozoa come into contact with the electrode (anode), an electron transfer reaction occurs between the cell and the electrode, and a redox reaction of intracellular coenzyme occurs. It is known that cell activity decreases. However, simply contacting the cells of microorganisms with the anode was difficult because it was difficult to bring all the microorganisms scattered in the water to be treated into contact with the anode, and there was no technology to be used. Is late.

【0003】一方、従来の殺菌方法は、被処理水を沸騰
させる方法や、塩素を注入する方法など、被処理水の全
体に作用して確実に殺菌するものであったから、上記電
解殺菌の如く被処理水のうち、殺菌作用を受けない部分
が存在するものは実用化路線から外されて来た。
[0003] On the other hand, the conventional disinfection method, such as a method of boiling the water to be treated and a method of injecting chlorine, acts on the whole of the water to be treated and surely sterilizes it. Among the water to be treated, those that have a portion that is not subjected to the bactericidal action have been removed from the practical use route.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、上記従
来の殺菌方法のうち、被処理水を沸騰させる方法におい
ては、沸騰させるために消費エネルギーが大きいこと
と、熱源の管理上問題があること、及び被処理水が沸騰
により特性が変化してしまうなどの欠点があって、用途
によっては適用出来ないことから、他の殺菌方法が求め
られてきた。
However, among the above-mentioned conventional sterilization methods, the method of boiling the water to be treated requires a large amount of energy for boiling, and has a problem in managing a heat source. Since there is a drawback that the water to be treated changes its properties due to boiling, and cannot be applied depending on the use, other sterilization methods have been required.

【0005】また、塩素を注入する方法は、広く水道水
の殺菌に適用されてきているが、多量の塩素を投入しな
ければならないことと、塩素臭が残るなどの欠点があ
る。これら従来実施されてきた技術を超して、電解殺菌
の方式が実用化され、そのメリットを発揮するには、色
々な実用上の問題を解消しなければならない。
Further, the method of injecting chlorine has been widely applied to sterilization of tap water, but has disadvantages such as a large amount of chlorine to be introduced and a chlorine odor remaining. Beyond these conventional techniques, the electrolytic sterilization method is put to practical use, and various practical problems must be solved in order to exert its merits.

【0006】この発明は、上記の問題を解決するもの
で、電解槽内に配置される電極に繊維状活性炭や多孔質
金属を設けて被処理水に含まれる細菌や原生動物等の微
生物を殺菌する電解殺菌装置を提供することを目的とし
たものである。
The present invention solves the above-mentioned problems, and provides fibrous activated carbon or porous metal to an electrode disposed in an electrolytic cell to sterilize microorganisms such as bacteria and protozoa contained in water to be treated. It is an object of the present invention to provide an electrolytic sterilization apparatus that performs the following.

【0007】[0007]

【課題を解決するための手段】請求項1の発明では、被
処理水をアノード電極とカソード電極とが対向して配置
された電解槽内に通液させて前記被処理水中の細菌や原
生動物等の微生物の殺菌を行う電解殺菌装置において、
前記アノード電極に筒型繊維状活性炭を、カソード電極
に網状或いは多孔質状の金属を設け、このアノード電極
を内側にカソード電極を外側に配置し、前記アノード電
極の表面積を多くして被処理水中の微生物の殺菌率を高
くするようにしている。
According to the first aspect of the present invention, the water to be treated is passed through an electrolytic cell in which an anode electrode and a cathode electrode are arranged to face each other, and the bacteria and protozoa in the water to be treated are passed through. In an electrolytic sterilizer that sterilizes microorganisms such as
A tubular fibrous activated carbon is provided for the anode electrode, and a reticulated or porous metal is provided for the cathode electrode. The anode electrode is disposed inside the cathode electrode outside, and the surface area of the anode electrode is increased by increasing the surface area of the anode electrode. The germicidal rate of microorganisms is increased.

【0008】請求項2の発明では、被処理水をアノード
電極とカソード電極とが対向して配置された電解槽内に
通液させて前記被処理水中の細菌や原生動物等の微生物
の殺菌を行う電解殺菌装置において、前記アノード電極
とカソード電極とに筒型繊維状活性炭を設け、このアノ
ード電極を内側にカソード電極を外側に配置し、電極を
反転した場合に一方の筒型繊維状活性炭の再生を図りな
がら他方の筒型繊維活性炭で殺菌を行えるようにしてい
る。
According to the second aspect of the present invention, the water to be treated is passed through an electrolytic cell in which an anode electrode and a cathode electrode are arranged opposite to each other to sterilize microorganisms such as bacteria and protozoa in the water to be treated. In the electrolytic sterilizer to be performed, a tubular fibrous activated carbon is provided on the anode electrode and the cathode electrode, and the anode electrode is disposed inside the cathode electrode on the outside, and when the electrode is inverted, one of the tubular fibrous activated carbons is used. While recycling, sterilization can be performed with the other tubular fiber activated carbon.

【0009】請求項3の発明では、アノード電極とカソ
ード電極との間の絶縁体でこのアノード電極とカソード
電極との短絡を防止できるようにしている。
According to the third aspect of the present invention, an insulator between the anode electrode and the cathode electrode can prevent a short circuit between the anode electrode and the cathode electrode.

【0010】請求項4の発明では、アノード電極とカソ
ード電極とをそれぞれ複層することにより殺菌率の向上
を図れるようにしている。
According to the fourth aspect of the present invention, the sterilization rate can be improved by forming the anode electrode and the cathode electrode in multiple layers.

【0011】[0011]

【発明の実施の形態】以下、この発明の実施例を図面に
基づいて説明する。図1は、この発明の電解処理槽の斜
視図である。図2は、この発明の電解処理槽の縦断面図
である。図3は、この発明の電解処理槽の横断面図であ
る。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a perspective view of the electrolytic treatment tank of the present invention. FIG. 2 is a longitudinal sectional view of the electrolytic treatment tank of the present invention. FIG. 3 is a cross-sectional view of the electrolytic treatment tank of the present invention.

【0012】1は電解処理槽で、この電解処理槽は本体
容器2と、この容器内に配置された細菌や原生動物等の
微生物を殺菌する殺菌装置3とで構成されている。
Reference numeral 1 denotes an electrolytic treatment tank. This electrolytic treatment tank comprises a main body container 2 and a sterilizer 3 disposed in the container for sterilizing microorganisms such as bacteria and protozoa.

【0013】殺菌装置3は同心状に配置した筒型繊維状
活性炭4と、筒型網状金属5と、この繊維状活性炭と網
状金属との上下端に設けた上板6と下板7とで形成され
ている。筒型繊維状活性炭4にはアノード電極が、筒型
網状金属5にはカソード電極がそれぞれ接続されてい
る。
The sterilizing apparatus 3 comprises a tubular fibrous activated carbon 4, a tubular reticulated metal 5, and an upper plate 6 and a lower plate 7 provided at the upper and lower ends of the fibrous activated carbon and the reticulated metal. Is formed. An anode electrode is connected to the tubular fibrous activated carbon 4, and a cathode electrode is connected to the tubular reticulated metal 5.

【0014】筒型繊維状活性炭4は筒型網状金属5の内
側に配置され、内部に被処理水を貯留する空間8を形成
している。そして、空間8内には本体容器2の上部中央
を貫通して取り付けられる被処理水の入口パイプ9が開
口している。また、筒型網状金属5の外側と本体容器2
との間の空間10には殺菌装置3を通過した被処理水を
本体容器2の外部に排出する出口パイプ11が開口して
いる。
The tubular fibrous activated carbon 4 is arranged inside the tubular reticulated metal 5 and forms a space 8 in which water to be treated is stored. In the space 8, an inlet pipe 9 for the water to be treated, which is attached so as to penetrate the upper center of the main body container 2, is opened. Further, the outside of the tubular mesh metal 5 and the main body container 2
An outlet pipe 11 for discharging the water to be treated that has passed through the sterilizer 3 to the outside of the main body container 2 is opened in the space 10 between the inside and the outside.

【0015】筒型繊維状活性炭4と筒型網状金属5との
間には内外を連通する孔12を有する樹脂製の板状の絶
縁体13が挟持されている。
Between the tubular fibrous activated carbon 4 and the tubular reticulated metal 5, a resin plate-like insulator 13 having a hole 12 communicating between the inside and outside is sandwiched.

【0016】アノード電極とカソード電極とは2ボルト
から5ボルト程度の直流電源14に接続され、陽極側の
アノード電極上で+0.74ボルトの殺菌に必要な電圧
を得るように制御している。
The anode electrode and the cathode electrode are connected to a DC power supply 14 of about 2 to 5 volts, and are controlled so that a voltage required for sterilization of +0.74 volts is obtained on the anode electrode on the anode side.

【0017】このように構成された電解処理装置におい
て、本体容器2の入口パイプ9を図示しない水道の蛇口
に接続し、出口パイプ11を図示しない自動販売機等の
飲料用のタンクに接続して設けられている。
In the electrolytic treatment apparatus thus constructed, the inlet pipe 9 of the main body container 2 is connected to a water tap (not shown), and the outlet pipe 11 is connected to a not-shown beverage tank such as a vending machine. Is provided.

【0018】水道の蛇口から入口パイプ9を介して電解
処理槽1内に供給された水道水は筒型繊維状活性炭4の
内側の空間8内に流入し、アノード電極に設けられた筒
型繊維状活性炭4に接触してこの繊維状活性炭の表面で
高電位のエネルギー供給を受け強力な酸化還元反応が水
道水に含まれている細菌や原生動物等の微生物の細胞内
で生じ、その活動が弱まって死滅して殺菌される。そし
て、水道水は筒型繊維状活性炭4を通過して筒型網状金
属5の外側の空間10内に流出して出口パイプ11から
外部に供給され、飲料用のタンク内に貯留されて利用さ
れる。
The tap water supplied from the tap to the electrolytic treatment tank 1 through the inlet pipe 9 flows into the space 8 inside the tubular fibrous activated carbon 4 and the tubular fiber provided on the anode electrode. The surface of the fibrous activated carbon comes in contact with the activated carbon 4 and receives a high-potential energy supply, and a strong oxidation-reduction reaction occurs in the cells of microorganisms such as bacteria and protozoa contained in tap water. Weak and die and are sterilized. Then, the tap water passes through the tubular fibrous activated carbon 4, flows out into the space 10 outside the tubular mesh metal 5, is supplied to the outside from the outlet pipe 11, and is stored and used in a drinking tank. You.

【0019】アノード電極の筒型繊維状活性炭4とカソ
ード電極との間の電圧は2ボルトから5ボルトの範囲に
して制御してアノード電極の表面の電位を+0.74ボ
ルトにして水道水が電解反応を起こさないようにすると
共に、水の電解反応による無駄な電力消費を抑え、か
つ、酸素と水素との発生による爆発の危険も回避してい
る。
The voltage between the tubular fibrous activated carbon 4 of the anode electrode and the cathode electrode is controlled in the range of 2 to 5 volts, the potential on the surface of the anode electrode is set to +0.74 volts, and tap water is electrolyzed. In addition to preventing the reaction from occurring, wasteful power consumption due to the electrolytic reaction of water is suppressed, and the danger of explosion due to generation of oxygen and hydrogen is also avoided.

【0020】筒型繊維状活性炭4は表面積を大きくする
ことにより、水道水に含まれている細菌や原生動物等の
微生物が接触する面を増やして電極での微生物の吸着性
能を向上するようにしている。
The tubular fibrous activated carbon 4 has an increased surface area to increase the surface of the tap water that comes into contact with microorganisms such as bacteria and protozoa, thereby improving the performance of adsorbing microorganisms on the electrode. ing.

【0021】樹脂製の絶縁体7はアノード電極とカソー
ド電極との間に挟持されることにより、前記アノード電
極とカソード電極との短絡を防止するようにしている。
The resin insulator 7 is sandwiched between the anode electrode and the cathode electrode to prevent a short circuit between the anode electrode and the cathode electrode.

【0022】電解処理槽1は入口パイプ9を水道の蛇口
に接続することにより、水道水自身の水圧で水が筒型繊
維状活性炭4を浸透して殺菌処理するようにしている。
また、蛇口に直結しない場合には、ポンプ等で被処理水
を加圧して筒型繊維状活性炭4に浸透させるようにして
いる。
In the electrolytic treatment tank 1, the inlet pipe 9 is connected to a tap for faucet so that the water permeates the tubular fibrous activated carbon 4 by the water pressure of the tap water itself and sterilizes it.
Further, when the water to be treated is not directly connected to the faucet, the water to be treated is pressurized by a pump or the like so as to permeate the tubular fibrous activated carbon 4.

【0023】アノード電極とカソード電極とに接続され
る直流電源は極性を反転させることにより、アノード電
極に設けられた筒型繊維状活性炭4が目ずまりを起こし
てもこの筒型繊維状活性炭に付着した死滅微生物を被処
理水に再溶解させて電極表面から除去して再生できるよ
うにしている。
The direct current power supply connected to the anode electrode and the cathode electrode inverts the polarity so that even if the tubular fibrous activated carbon 4 provided on the anode electrode is clogged, the tubular fibrous activated carbon 4 The attached dead microorganisms are redissolved in the water to be treated, removed from the electrode surface, and regenerated.

【0024】尚、上記説明においては、アノード電極に
筒型繊維状活性炭4を、カソード電極に筒型網状金属5
を用いて説明したが、カソード電極の金属を発泡金属等
の多孔質金属で形成しても同等の効果を有する。また、
図4に示すようにアノード電極とカソード電極との両方
に筒型繊維状活性炭15、16を用いた場合にはアノー
ド電極とカソード電極との極性を反転させたときに、再
生をさせつつ細菌や原生動物等の微生物の殺菌処理を行
うことができるので、電解処理槽1を長時間にわたり連
続運転を行わせる効果を有する。
In the above description, the tubular fibrous activated carbon 4 is used for the anode electrode and the tubular reticulated metal 5 is used for the cathode electrode.
However, even if the metal of the cathode electrode is formed of a porous metal such as a foamed metal, the same effect can be obtained. Also,
As shown in FIG. 4, when the tubular fibrous activated carbon 15, 16 is used for both the anode electrode and the cathode electrode, when the polarity of the anode electrode and the cathode electrode is reversed, bacteria and Since the sterilization treatment of microorganisms such as protozoa can be performed, there is an effect that the electrolytic treatment tank 1 can be continuously operated for a long time.

【0025】更に、図5のようにアノード電極とカソー
ド電極とをそれそれ複層させることで、被処理水中の微
生物の除去能力を向上させられることは言うまでもな
い。
Further, it is needless to say that the ability to remove microorganisms in the water to be treated can be improved by forming a plurality of anode electrodes and cathode electrodes as shown in FIG.

【0026】[0026]

【発明の効果】以上のように請求項1の発明によれば、
被処理水をアノード電極とカソード電極とが対向して配
置された電解槽内に通液させて前記被処理水中の細菌や
原生動物等の微生物の殺菌を行う電解殺菌装置におい
て、前記アノード電極に筒型繊維状活性炭を、カソード
電極に網状或いは多孔質状の金属を設け、このアノード
電極を内側にカソード電極を外側に配置したので、前記
被処理水の接触する前記アノード電極の表面積が多く、
この被処理水中の微生物の殺菌を効率的に行うことがで
きる。
As described above, according to the first aspect of the present invention,
In an electrolytic sterilization apparatus for sterilizing microorganisms such as bacteria and protozoa in the water to be treated by passing the water to be treated through an electrolytic cell in which an anode electrode and a cathode electrode are arranged opposite to each other, The tubular fibrous activated carbon, a mesh-like or porous metal is provided on the cathode electrode, and the anode electrode is arranged inside the anode electrode, so that the surface area of the anode electrode in contact with the water to be treated is large,
The microorganisms in the water to be treated can be efficiently sterilized.

【0027】請求項2の発明によれば、被処理水をアノ
ード電極とカソード電極とが対向して配置された電解槽
内に通液させて前記被処理水中の細菌や原生動物等の微
生物の殺菌を行う電解殺菌装置において、前記アノード
電極とカソード電極とに筒型繊維状活性炭を設け、この
アノード電極を内側にカソード電極を外側に配置したの
で、電極を反転した場合に一方の筒型繊維状活性炭の再
生を図りながら他方の筒型繊維状活性炭で殺菌を行うこ
とができる。
According to the second aspect of the present invention, the water to be treated is passed through the electrolytic cell in which the anode electrode and the cathode electrode are arranged opposite to each other to remove microorganisms such as bacteria and protozoa in the water to be treated. In the electrolytic sterilizer for sterilization, a tubular fibrous activated carbon is provided on the anode electrode and the cathode electrode, and the anode electrode is arranged inside the cathode electrode outside, so that when the electrode is inverted, one of the tubular fibers is turned off. Sterilization can be performed with the other tubular fibrous activated carbon while regenerating the activated carbon.

【0028】請求項3の発明によれば、アノード電極と
カソード電極との間に挟持した絶縁体でこのアノード電
極とカソード電極との短絡を防止でき、各電極の取付管
理を簡略化することができる。
According to the third aspect of the present invention, a short circuit between the anode electrode and the cathode electrode can be prevented by the insulator sandwiched between the anode electrode and the cathode electrode, and the mounting management of each electrode can be simplified. it can.

【0029】請求項4の発明によれば、アノード電極と
カソード電極とをそれぞれ複層することにより細菌や原
生動物等の微生物が前記アノード電極の筒状繊維状活性
炭を複数回通過することで電極との接触の確率を高めて
殺菌率の向上を図れることができる。
According to the fourth aspect of the present invention, the anode electrode and the cathode electrode are respectively multi-layered so that microorganisms such as bacteria and protozoa pass through the tubular fibrous activated carbon of the anode electrode a plurality of times. The probability of contact with the metal can be increased to improve the sterilization rate.

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

【図1】この発明の電解処理槽の斜視図である。FIG. 1 is a perspective view of an electrolytic treatment tank according to the present invention.

【図2】この発明の電解処理槽の縦断面図である。FIG. 2 is a longitudinal sectional view of the electrolytic treatment tank of the present invention.

【図3】この発明の電解処理槽の横断面図である。FIG. 3 is a cross-sectional view of the electrolytic treatment tank of the present invention.

【図4】この発明の他の実施例を示す電解処理槽の縦断
面図である。
FIG. 4 is a longitudinal sectional view of an electrolytic treatment tank showing another embodiment of the present invention.

【図5】この発明のその他の実施例を示す電解処理槽の
縦断面図である。
FIG. 5 is a longitudinal sectional view of an electrolytic treatment tank showing another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 電解処理槽 4、15、16 筒型繊維状活性炭 5 筒型網状金属 13 絶縁体 Reference Signs List 1 electrolytic treatment tank 4, 15, 16 tubular fibrous activated carbon 5 tubular reticulated metal 13 insulator

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 被処理水をアノード電極とカソード電極
とが対向して配置された電解槽内に通液させて前記被処
理水中の細菌や原生動物等の微生物の殺菌を行う電解殺
菌装置において、前記アノード電極に筒型繊維状活性炭
を、カソード電極に網状或いは多孔質状の金属を設け、
このアノード電極を内側にカソード電極を外側に配置し
たことを特徴とする電解殺菌装置。
1. An electrolytic sterilizer for sterilizing microorganisms such as bacteria and protozoa in the water to be treated by flowing the water to be treated into an electrolytic cell in which an anode electrode and a cathode electrode are arranged to face each other. A tubular fibrous activated carbon is provided for the anode electrode, and a mesh or porous metal is provided for the cathode electrode,
An electrolytic sterilizer comprising the anode electrode disposed inside and the cathode electrode disposed outside.
【請求項2】 被処理水をアノード電極とカソード電極
とが対向して配置された電解槽内に通液させて前記被処
理水中の細菌や原生動物等の微生物の殺菌を行う電解殺
菌装置において、前記アノード電極とカソード電極とに
筒型繊維状活性炭を設け、このアノード電極を内側にカ
ソード電極を外側に配置したことを特徴とする電解殺菌
装置。
2. An electrolytic disinfection apparatus for sterilizing microorganisms such as bacteria and protozoa in the water to be treated by passing the water to be treated through an electrolytic cell in which an anode electrode and a cathode electrode are arranged opposite to each other. An electrolytic sterilizer comprising: a tubular fibrous activated carbon provided on the anode electrode and the cathode electrode; and the anode electrode is disposed inside and the cathode electrode is disposed outside.
【請求項3】 アノード電極とカソード電極との間に絶
縁体を介在させたことを特徴とする請求項1及び2に記
載された電解殺菌装置。
3. The electrolytic sterilizer according to claim 1, wherein an insulator is interposed between the anode electrode and the cathode electrode.
【請求項4】 アノード電極とカソード電極とを交互に
複数形成したことを特徴とする請求項1及び2に記載さ
れた電解殺菌装置。
4. The electrolytic sterilizer according to claim 1, wherein a plurality of anode electrodes and cathode electrodes are alternately formed.
JP10202280A 1998-07-16 1998-07-16 Electrolytic sterilizer Pending JP2000033379A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10202280A JP2000033379A (en) 1998-07-16 1998-07-16 Electrolytic sterilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10202280A JP2000033379A (en) 1998-07-16 1998-07-16 Electrolytic sterilizer

Publications (1)

Publication Number Publication Date
JP2000033379A true JP2000033379A (en) 2000-02-02

Family

ID=16454931

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10202280A Pending JP2000033379A (en) 1998-07-16 1998-07-16 Electrolytic sterilizer

Country Status (1)

Country Link
JP (1) JP2000033379A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005279538A (en) * 2004-03-30 2005-10-13 Hiroyuki Yoshida Water modifying method in making electrolytic water, and electrolytic water making apparatus
JP2007021490A (en) * 2005-06-17 2007-02-01 Yoshitoshi Maeda Treatment method and treatment apparatus of water
JP2008062234A (en) * 2007-10-19 2008-03-21 Tokyo Yogyo Co Ltd Electrolytic water purifier
CN102491458A (en) * 2011-11-24 2012-06-13 厦门绿信环保科技有限公司 Microorganism killing device for circulating water
CN103435110A (en) * 2013-08-16 2013-12-11 上海元清环保科技有限公司 Electrolytic catalyzing adsorbent filter
JP2016022469A (en) * 2014-07-24 2016-02-08 中国電力株式会社 Device for generating hydrogen-containing water, and bathing facility
JP2016516577A (en) * 2013-04-25 2016-06-09 ラディカル フィルトレーション リミテッドRadical Filtration Limited Electrochemical filter device
CN117023916A (en) * 2023-10-09 2023-11-10 潍坊市人民医院(潍坊市公共卫生临床中心) Medical sewage treatment device and method

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005279538A (en) * 2004-03-30 2005-10-13 Hiroyuki Yoshida Water modifying method in making electrolytic water, and electrolytic water making apparatus
JP4605694B2 (en) * 2004-03-30 2011-01-05 株式会社テックコーポレーション Water quality improvement method and electrolyzed water generating apparatus in electrolyzed water generation
JP2007021490A (en) * 2005-06-17 2007-02-01 Yoshitoshi Maeda Treatment method and treatment apparatus of water
JP2008062234A (en) * 2007-10-19 2008-03-21 Tokyo Yogyo Co Ltd Electrolytic water purifier
CN102491458A (en) * 2011-11-24 2012-06-13 厦门绿信环保科技有限公司 Microorganism killing device for circulating water
JP2016516577A (en) * 2013-04-25 2016-06-09 ラディカル フィルトレーション リミテッドRadical Filtration Limited Electrochemical filter device
CN103435110A (en) * 2013-08-16 2013-12-11 上海元清环保科技有限公司 Electrolytic catalyzing adsorbent filter
JP2016022469A (en) * 2014-07-24 2016-02-08 中国電力株式会社 Device for generating hydrogen-containing water, and bathing facility
CN117023916A (en) * 2023-10-09 2023-11-10 潍坊市人民医院(潍坊市公共卫生临床中心) Medical sewage treatment device and method
CN117023916B (en) * 2023-10-09 2024-04-09 潍坊市人民医院(潍坊市公共卫生临床中心) Medical sewage treatment device and method

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