JPH10113665A - Electrode for electrolytically oxidizing water - Google Patents

Electrode for electrolytically oxidizing water

Info

Publication number
JPH10113665A
JPH10113665A JP30231796A JP30231796A JPH10113665A JP H10113665 A JPH10113665 A JP H10113665A JP 30231796 A JP30231796 A JP 30231796A JP 30231796 A JP30231796 A JP 30231796A JP H10113665 A JPH10113665 A JP H10113665A
Authority
JP
Japan
Prior art keywords
anode
water
cathode
electrode
nonwoven fabric
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
JP30231796A
Other languages
Japanese (ja)
Inventor
Kenichi Fujita
賢一 藤田
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 JP30231796A priority Critical patent/JPH10113665A/en
Publication of JPH10113665A publication Critical patent/JPH10113665A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide an electrode to be used when the water contg. org. matter, bacteria, etc., is purified by electrolytic oxidation. SOLUTION: A nonwoven-fabric filter 3 is held between an anode 1 and a cathode 2 in contact with the water inlet-side face of the anode 1 to constitute the electrode. The anode 1 and cathode 2 consist of a water-permeable metallic sheet, especially a metallic sheet excellent in oxidation resistance, since active oxygen is generated on the anode surface. Ti is preferably used as the anode material, and the oxidation resistance is further improved by a platinum plating. The nonwoven fabric 3 held between the anode 1 and cathode 2 can be made of the resin, metal, ceramic and conductive or nonconductive material. The nonwoven fabric 3 acts as one kind of filter medium, and the suspended org. matter separated by filtration and blocked by the front of the nonwoven fabric is oxidized by the oxygen generated on the anode and burned. The water current is introduced from the cathode 2, filtered by the nonwoven fabric 3, passed through the anode 1 and discharged to the outside.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、水の電解酸化電極にか
かわり、さらに詳しくは、有機物や雑菌類等を含んだ浴
用水、生簀の水、活魚水槽の水、ビル、マンションの給
水用循環水、プールの水、湖沼の水、等々、いわゆる循
環、貯槽して使用する水を電解酸化によって浄化する際
の酸化電極の構造に係わるものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electro-oxidation electrode for water, and more particularly to bath water containing organic matter and various germs, water for fish cages, water for live fish tanks, and water supply circulation for buildings and condominiums. The present invention relates to the structure of an oxidation electrode when purifying water used in circulation, storage, and the like, such as water, pool water, and lake water, by electrolytic oxidation.

【0002】[0002]

【従来の技術】通水性の炭素電極を使って循環水を電解
酸化、浄化することは本発明者が発明し、すでに出願し
ている。この方法によると、活魚水槽の魚の排泄物、浴
用水の有機物、その他有機物を含んだ水の中の有機物を
酸化、分解できることが判明した。しかしながら一つ問
題があった。これは電解酸化する際の電流密度を上げる
と、たしかに有機物の分解速度は増加するが、電流の増
加に伴い、炭素電極の表面も電解酸化を受けて、表面か
らコロイド状の炭素微粉が析出して水が黒く変色するこ
とである。炭素の析出そのものは別に害はないが、水が
黒く変色するために、とくに循環、貯槽使用する用途で
は問題があった。炭素微粉の析出をなくすためには電極
材料として炭素以外の耐酸化性金属を使用しなければな
らないが、金属で炭素材に匹敵するような濾過材を形成
するのは高価すぎて価格的に困難であった。
2. Description of the Related Art The present inventors have invented and have already filed an application for electrolytically oxidizing and purifying circulating water using a water-permeable carbon electrode. According to this method, it was found that excrement of fish in the live fish tank, organic matter in bath water, and other organic matter in water containing organic matter can be oxidized and decomposed. However, there was one problem. If the current density during electrolytic oxidation is increased, the decomposition rate of organic matter will certainly increase, but with the increase in current, the surface of the carbon electrode also undergoes electrolytic oxidation, and colloidal carbon fines precipitate from the surface. The water turns black. Although the deposition of carbon itself is not harmful, there is a problem particularly in applications where circulation and storage tanks are used because water turns black. In order to eliminate the deposition of carbon fines, an oxidation-resistant metal other than carbon must be used as an electrode material, but it is too expensive to form a filter material that is comparable to carbon material with metal, which is too expensive Met.

【0003】[0003]

【発明が解決する課題】本発明は、かかる状況に鑑みて
なされたもので、その目的とするところは、上記した問
題点を解決した新しい方法を提供せんとするものであ
る。
SUMMARY OF THE INVENTION The present invention has been made in view of such circumstances, and an object of the present invention is to provide a new method which solves the above-mentioned problems.

【0004】[0004]

【課題を解決するための手段】上記問題点は次の手段に
よって解決される。 1.通水性のある耐酸化性金属板からなる金属陽極と陰
極の間に、該陽極の水の流入側の面に接して、不織布フ
ィルターを挟んでなることを特徴とする水の電解酸化電
極。 2.上記陽極材料が、チタンである1に記載の電極。 3.上記陽極表面に白金がメッキされてなる2に記載の
電極。
The above problems are solved by the following means. 1. A water electro-oxidation electrode comprising a non-woven fabric filter sandwiched between a metal anode and a cathode formed of a water-permeable oxidation-resistant metal plate and in contact with the water inflow side of the anode. 2. 2. The electrode according to 1, wherein the anode material is titanium. 3. 3. The electrode according to 2, wherein the surface of the anode is plated with platinum.

【0005】[0005]

【発明の実施の形態】本発明に使用する電極の要部は3
層構造からなる。すなわち、陽極と陰極の間、陽極の水
の流入側の面に接して、不織布フィルターが挟まれた構
造からなる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The main part of the electrode used in the present invention is 3
It has a layer structure. That is, the nonwoven fabric filter is sandwiched between the anode and the cathode, in contact with the surface of the anode on the water inflow side.

【0006】陽極、陰極は共に、通水性のある金属板か
らなり、とく陽極表面には活性な酸素が発生するので耐
酸化性に優れた金属板からなる。陽極材料はTiが好ま
しく、白金をメッキするとさらに耐酸化性が向上する。
Both the anode and the cathode are made of a water-permeable metal plate, and in particular, are made of a metal plate having excellent oxidation resistance because active oxygen is generated on the surface of the anode. The anode material is preferably Ti, and when plated with platinum, the oxidation resistance is further improved.

【0007】陽極、陰極の間に挟む不織布は樹脂、金
属、セラミック、導電性、非導電性いずれの材料でもよ
い。不織布は一種の濾過材として働き、濾別され、不織
布前面に塞き止められた水中の浮遊有機物は陽極に発生
する酸素によって酸化されて燃焼する。水の流れは、陰
極から入り、不織布で濾別され、陽極を通って外に出
る。
The nonwoven fabric sandwiched between the anode and the cathode may be made of resin, metal, ceramic, conductive or non-conductive material. The nonwoven fabric acts as a kind of filter material, is separated by filtration, and the suspended organic matter in the water blocked on the front surface of the nonwoven fabric is oxidized by oxygen generated at the anode and burns. The stream of water enters at the cathode, is filtered through a nonwoven, and exits through the anode.

【0008】酸化電流は、面積200cmで概ね50
0〜2000mA程度が一つの目安であるが、有機物の
大きさによって目の粗さ、および全電流値を調節すれ
ば、循環水の有機物を効率よく酸化消滅させることがで
きる。
The oxidation current is approximately 50 for an area of 200 cm 2.
One standard is about 0 to 2000 mA, but if the coarseness and the total current value are adjusted according to the size of the organic matter, the organic matter in the circulating water can be efficiently oxidized and eliminated.

【0009】本発明方法は循環式浴用水、つまり24時
間使用できる循環式浴用水の浄化、食品排水の浄化、養
殖水槽の浄化、プール、湖沼の浄化、水の消臭、脱色、
水中の農薬の分解、水田の雑草、こけ、藻の発生防止に
効果がある。
[0009] The method of the present invention is a method of purifying circulating bath water, ie, circulating bath water which can be used for 24 hours, purifying food wastewater, purifying aquaculture tanks, purifying pools and lakes, deodorizing water, decolorizing water, and the like.
It is effective in breaking down pesticides in water and preventing weeds, moss and algae in paddy fields.

【0010】図面によって本発明の構造を説明する。図
1〜4は本発明構造の説明図である。図1〜2で、図1
は斜視図、図2は断面構造の説明図である。1は通水性
のTi陽極、2は通水性のステンレス(SUS304)
陰極である。3は1と2の間に挿入された不織布フィル
ターである。1のTi陽極には必要に応じて白金がメッ
キされる。水は陰極2側から入り、不織布3を通過して
陽極1に入り、陽極内面を抜けて出口から出る。不織布
フィルターは水の圧力に押されて1の陽極に押し付けら
れている。1の陽極面には活性酸素が発生しており、不
織布で塞き止められた有機物質は発生する酸素によって
酸化を受けて分解される。つまり一種の燃焼が起こり炭
酸ガスと窒素あるいは窒素酸化物になって気散する。本
発明の基本的構造は図1〜2の構造が代表するが、必要
に応じて陰極の外周にさらに通水性Ti陽極を配置して
もよい。図3〜4はこの場合の説明図である。
The structure of the present invention will be described with reference to the drawings. 1 to 4 are explanatory views of the structure of the present invention. 1 and FIG.
Is a perspective view, and FIG. 2 is an explanatory view of a cross-sectional structure. 1 is a water-permeable Ti anode, 2 is a water-permeable stainless steel (SUS304)
It is a cathode. 3 is a nonwoven fabric filter inserted between 1 and 2. One Ti anode is plated with platinum as needed. Water enters from the cathode 2 side, passes through the nonwoven fabric 3 and enters the anode 1, passes through the inner surface of the anode and exits through the outlet. The nonwoven filter is pressed against one anode by the pressure of water. Active oxygen is generated on the anode surface of No. 1, and the organic substance blocked by the nonwoven fabric is decomposed by oxidation by the generated oxygen. In other words, a kind of combustion occurs and gas is diffused into carbon dioxide and nitrogen or nitrogen oxides. Although the basic structure of the present invention is represented by the structures shown in FIGS. 1 and 2, if necessary, a water-permeable Ti anode may be further arranged on the outer periphery of the cathode. 3 and 4 are explanatory diagrams in this case.

【0011】[0011]

【実施例】【Example】

実施例1 図1〜2の構造の電極を使用して水の酸化処理をした。 Ti陽極の寸法:直径90mm,長さ110mm 通水孔の孔径: 0.5 mm、通水孔の面積率: 60% ステンレス陰極:直径110mm,長さ110mm 孔の孔径: 0.5mm、通水孔の面積率: 60% 陽極、陰極管の距離:3.5mm 不織布: 樹脂繊維の不織布 繊維の径100μm Example 1 Water oxidation treatment was performed using the electrodes having the structures shown in FIGS. Dimensions of Ti anode: diameter 90 mm, length 110 mm Hole diameter of water passage hole: 0.5 mm, area ratio of water passage hole: 60% Stainless steel cathode: diameter 110 mm, length 110 mm Hole diameter of hole: 0.5 mm, water passage Area ratio of holes: 60% Distance between anode and cathode tubes: 3.5 mm Non-woven fabric: Non-woven fabric of resin fiber Fiber diameter 100 μm

【0012】<浴用水への適用>ステンレスの陰極側か
ら浴用水を循環させた。 電流 :1000mA 20日間テストした。入浴者の延べ人数は、100人。 結果 不織布、チタン電極には、へどろ状の堆積物は皆無であ
った。有機物は完全に分解されたことが確認できた。ま
た、浴用水の大腸菌は検出されなかった。浴槽に湯垢の
付着もなかった。
<Application to Bath Water> Bath water was circulated from the cathode side of stainless steel. Current: 1000 mA Tested for 20 days. The total number of bathers is 100. Results There was no sludge-like deposit on the nonwoven fabric and the titanium electrode. It was confirmed that the organic matter was completely decomposed. Escherichia coli in bath water was not detected. There was no scale on the bathtub.

【0013】実施例2(農薬水の処理) 実施例1と同じ電解装置を使用した。30リットルのミ
ズに(ジメチルジカルベトキシエチルジチオホスフェー
ト)を15cc混ぜたミズを一昼夜循環させた。 <結果>農薬は検出されなかった。農薬で白く濁ってい
た水は透明になった。
Example 2 (Treatment of pesticide water) The same electrolytic apparatus as in Example 1 was used. A mixture of 15 liters of (dimethyl dicarbethoxyethyl dithiophosphate) in 30 liters of water was circulated all day and night. <Results> Pesticides were not detected. The water, which was cloudy white with pesticides, became clear.

【0014】実施例3(アンモニアの消臭) 実施例1と同じ電解装置を使用した。アンモニア臭のあ
る水を一昼夜電解した。アンモニア臭はまったくなくな
った。
Example 3 (Deodorization of ammonia) The same electrolytic apparatus as in Example 1 was used. Water with ammonia smell was electrolyzed all day and night. The smell of ammonia was completely gone.

【0015】実施例4(水のヌメリの除去) 実施例1と同じ電解装置を使用した。ヌメリの激しくな
った浴槽の水についてテストした。実施例1と同じ電解
装置を使用した。6時間処理した。ヌメリが取れてサラ
サラになった。
Example 4 (Removal of water slime) The same electrolytic apparatus as in Example 1 was used. The slime of the slime was tested on the bath water. The same electrolytic device as in Example 1 was used. Treated for 6 hours. The slime was removed and it became smooth.

【0016】実施例5(クーリングタワーの循環水) 実施例1と同じ電解装置を使用した。 テスト期間12カ月 パイプの内面に水垢の付着はまったくなかった。パイプ
に赤錆の発生もなかった。
Example 5 (Circulating water of cooling tower) The same electrolytic apparatus as in Example 1 was used. Test period 12 months No scale was deposited on the inside of the pipe. There was no red rust on the pipe.

【0017】実施例6(有機溶剤の混ざった水の処理) 実施例1と同じ電解装置を使用した。トリクロロエチレ
ンが1ppm検出された水を処理した。 時間:1昼夜 結果 トリクロロエチレンは検出されなかった。
Example 6 (Treatment of water mixed with an organic solvent) The same electrolytic apparatus as in Example 1 was used. The water in which 1 ppm of trichlorethylene was detected was treated. Time: Day / Night Results Trichlorethylene was not detected.

【0018】[0018]

【発明の効果】本発明は、以上詳記したように有機物を
高電流で高速酸化できるものであり、水資源の有効利用
に多大な貢献をなすものである。 <用途例> 1. 風呂の水の浄化 2. 熱交換器の循環水 3. 循環式冷却水 4. ソーラーシステム 5. ビルの給水、水道等、各種給排水設備 6. 各種冷却水のスケール、赤錆対策 7. スイミングプール 8. 下水処理、産業廃水処理 9. ゴルフ場の廃水処理 10.水族館、かつぎょ水槽の水処理 11.池の水の浄化処理
As described in detail above, the present invention is capable of oxidizing organic substances at a high current and at a high speed, and greatly contributes to effective use of water resources. <Application example> 1. Purification of bath water 2. 2. Circulating water of heat exchanger Circulating cooling water 4. Solar system 5. 5. Various water supply and drainage facilities such as water supply and water supply for buildings. 6. Various cooling water scales, measures against red rust Swimming pool 8. Sewage treatment, industrial wastewater treatment 9. Golf course wastewater treatment 10. Water treatment of aquariums and water tanks Pond water purification

【0019】[0019]

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

【図1】図1は本発明の構造を説明した図(斜視図)で
ある。
FIG. 1 is a diagram (perspective view) illustrating the structure of the present invention.

【図2】図2は本発明の構造を説明した図(断面図)で
ある。
FIG. 2 is a diagram (cross-sectional view) illustrating the structure of the present invention.

【図3】図3は本発明の別の構造を説明した図(斜視
図)である。
FIG. 3 is a view (perspective view) illustrating another structure of the present invention.

【図4】図4は本発明の別の構造を説明した図(断面
図)である。
FIG. 4 is a diagram (cross-sectional view) illustrating another structure of the present invention.

【符号の説明】[Explanation of symbols]

1 Ti陽極 2 ステンレス(SUS304)陰極 3 不織布フィルター 1 Ti anode 2 Stainless steel (SUS304) cathode 3 Non-woven fabric filter

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】通水性のある耐酸化性金属板からなる金属
陽極と陰極の間、該陽極の水の流入側の面に接して、不
織布フィルターを挟んでなることを特徴とする水の電解
酸化電極。
1. A method of electrolysis of water, comprising a nonwoven fabric filter interposed between a metal anode and a cathode made of a water-permeable oxidation-resistant metal plate, in contact with the surface of the anode on the water inflow side. Oxidation electrode.
【請求項2】上記陽極材料が、チタンである請求項1に
記載の電極。
2. The electrode according to claim 1, wherein said anode material is titanium.
【請求項3】上記陽極表面に白金がメッキされてなる請
求項2に記載の電極。
3. The electrode according to claim 2, wherein said anode surface is plated with platinum.
JP30231796A 1996-10-08 1996-10-08 Electrode for electrolytically oxidizing water Pending JPH10113665A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30231796A JPH10113665A (en) 1996-10-08 1996-10-08 Electrode for electrolytically oxidizing water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30231796A JPH10113665A (en) 1996-10-08 1996-10-08 Electrode for electrolytically oxidizing water

Publications (1)

Publication Number Publication Date
JPH10113665A true JPH10113665A (en) 1998-05-06

Family

ID=17907498

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30231796A Pending JPH10113665A (en) 1996-10-08 1996-10-08 Electrode for electrolytically oxidizing water

Country Status (1)

Country Link
JP (1) JPH10113665A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19844329A1 (en) * 1998-09-28 2000-03-30 Univ Schiller Jena Water with biological impurities electrolytically treated in titanium oxide catalytic reactor, process deals efficiently with large quantities with reproducible results
KR100858172B1 (en) 2007-02-22 2008-09-10 최영철 Oxygen generator by titanium foam, Oxygen water purifier and Oxygen water bathtub device using the same

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19844329A1 (en) * 1998-09-28 2000-03-30 Univ Schiller Jena Water with biological impurities electrolytically treated in titanium oxide catalytic reactor, process deals efficiently with large quantities with reproducible results
DE19844329B4 (en) * 1998-09-28 2010-06-17 Friedrich-Schiller-Universität Jena Process for the treatment of microorganisms and pollutants
KR100858172B1 (en) 2007-02-22 2008-09-10 최영철 Oxygen generator by titanium foam, Oxygen water purifier and Oxygen water bathtub device using the same

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