JPH1110160A - Method for treating water by electrolytic oxidation - Google Patents
Method for treating water by electrolytic oxidationInfo
- Publication number
- JPH1110160A JPH1110160A JP16469197A JP16469197A JPH1110160A JP H1110160 A JPH1110160 A JP H1110160A JP 16469197 A JP16469197 A JP 16469197A JP 16469197 A JP16469197 A JP 16469197A JP H1110160 A JPH1110160 A JP H1110160A
- Authority
- JP
- Japan
- Prior art keywords
- water
- electrolytic
- activated carbon
- waste liquid
- composite material
- 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
Links
Landscapes
- Apparatus For Disinfection Or Sterilisation (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術の分野】本発明は、電解酸化分解を
利用した廃液処理方法、浄水生成方法および電解水生成
方法等の水処理方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water treatment method such as a waste liquid treatment method utilizing electrolytic oxidative decomposition, a purified water producing method, and an electrolytic water producing method.
【0002】[0002]
【従来の技術】産業廃液による自然環境破壊を防止する
ため、廃液中に含まれる有機物等の効果的、即効的、経
済的な除去方法が求められている。従来の方法として
は、たとえば生物分解する方法、あるいは次亜塩素酸ナ
トリウムにより化学分解する方法等がある。さらに、特
開平2−131184号公報には有機物を活性炭に吸着
させて除去する方法が、また、同7−265862、同
8−281271、同8−296081各号公報には、
電気分解による除去方法が示されている。2. Description of the Related Art In order to prevent the destruction of the natural environment by industrial waste liquid, there is a demand for an effective, immediate and economical method for removing organic substances and the like contained in the waste liquid. Conventional methods include, for example, a biodegradation method and a chemical decomposition method using sodium hypochlorite. Further, JP-A-2-131184 discloses a method of adsorbing and removing organic substances on activated carbon, and JP-A-7-265860, JP-A-8-281271 and JP-A-8-296081 disclose a method.
An electrolysis removal method is shown.
【0003】また、水道水には、塩素を中心とする殺菌
剤が大量に投入されている。その結果、水道水には発ガ
ン性を指摘されているトリハロメタン類が含有されてお
り、その除去が必要とされている。そのような浄水生成
装置には、一般的に活性炭層と中空糸膜層が一体となっ
たカートリッジ等が広く用いられている。[0003] In addition, a large amount of disinfectant mainly containing chlorine is supplied to tap water. As a result, tap water contains trihalomethanes, which have been pointed out as carcinogenic, and their removal is required. In such a water purification device, generally, a cartridge or the like in which an activated carbon layer and a hollow fiber membrane layer are integrated is widely used.
【0004】また、食品用、医療・衛生用の各種機器の
洗浄、殺菌方法としては、次亜塩素酸ナトリウム水溶液
を殺菌水として用いるのが一般的である。また最近で
は、特開平8−308910号公報に記載されているよ
うな、電解殺菌による方法も行われている。電解殺菌の
際の電極としては、一般的に白金等が使われている。As a method for washing and sterilizing various food and medical / hygiene equipment, an aqueous sodium hypochlorite solution is generally used as sterilizing water. Recently, a method using electrolytic sterilization as described in JP-A-8-308910 has also been used. In general, platinum or the like is used as an electrode for electrolytic sterilization.
【0005】[0005]
【発明が解決しようとする課題】上記のような従来の水
処理方法には種々の問題があり、いずれも満足の得られ
るものではない。The above-mentioned conventional water treatment methods have various problems and none of them is satisfactory.
【0006】すなわち、生物分解の方法は、分解時間が
非常に長いという問題点がある。また、次亜塩素酸ナト
リウムによる化学分解の方法では、次亜塩素酸ナトリウ
ムの再生利用ができないため、ランニングコストがかさ
むという問題点がある。さらに、上記の特開平2−13
1184号公報記載のような活性炭に吸着させる方法で
は、活性炭の再利用効率が悪いため、コストが非常に高
くなるという問題点がある。That is, the biodegradation method has a problem that the decomposition time is very long. Further, in the method of chemical decomposition using sodium hypochlorite, there is a problem that the running cost is increased because sodium hypochlorite cannot be recycled. Further, Japanese Patent Application Laid-Open No.
In the method of adsorbing on activated carbon as described in Japanese Patent No. 1184, there is a problem that the cost is extremely high because the activated carbon is not efficiently reused.
【0007】また、上記の特開平8−281271、お
よび同8−296081各号公報に記載の電気分解法の
場合は、電極に白金、二酸化ルテニウム、二酸化鉛、二
酸化スズ、ステンレス、黒鉛等が使われているが、黒鉛
以外の金属材料は、徐々に腐食されて、有毒性材料とし
て流出するという問題点がある。In the case of the electrolysis method described in the above-mentioned JP-A-8-281271 and JP-A-8-296081, platinum, ruthenium dioxide, lead dioxide, tin dioxide, stainless steel, graphite and the like are used for electrodes. However, there is a problem that metal materials other than graphite are gradually corroded and flow out as toxic materials.
【0008】黒鉛の場合は、腐食はないものの、摩耗が
激しく、高い電流密度での処理ができないという問題点
がある。また、特開平7−265862号公報には電極
の接触面積を増加させる目的で、活性炭粉末をネットの
中に充填して陽極の補助電極とする方法が示されてい
る。[0008] In the case of graphite, although there is no corrosion, there is a problem that it is severely worn and cannot be processed at a high current density. In addition, Japanese Patent Application Laid-Open No. 7-265862 discloses a method in which activated carbon powder is filled in a net to form an auxiliary electrode of an anode in order to increase the contact area of the electrode.
【0009】しかしながら、活性炭粉末をネット等によ
り被覆した構造の電極では、非常に接触抵抗が高く、ま
たネットから細かい粉末が飛散するという問題点があ
る。However, an electrode having a structure in which activated carbon powder is covered with a net or the like has problems that the contact resistance is extremely high and fine powder scatters from the net.
【0010】また、活性炭層と中空糸膜層が一体構造を
なしたカートリッジを用いる浄水生成装置の場合は、浄
水効率が低下すると、カートリッジの交換を行わなけれ
ばならないため、資源の無駄が多くなるいう問題点があ
る。また、カートリッジは徐々に汚染された状態で使用
されるため、有害菌類が繁殖し、衛生上重大な問題にも
なっている。[0010] In the case of a water purification apparatus using a cartridge in which the activated carbon layer and the hollow fiber membrane layer have an integral structure, if the water purification efficiency is reduced, the cartridge must be replaced, which wastes resources. There is a problem. Further, since the cartridge is used in a gradually contaminated state, harmful fungi proliferate, which is a serious hygiene problem.
【0011】また、食品や医療関係の殺菌処理に一般的
に用いられている次亜塩素酸ナトリウム水溶液は、前記
のように再生できないためにランニングコストがかさむ
だけでなく、化学的に不安定で長期保存ができず、また
適正な濃度管理も困難であるという問題点がある。The aqueous sodium hypochlorite solution generally used for sterilization treatment of foods and medical treatments cannot be regenerated as described above, so that not only the running cost is increased, but also chemically unstable. There is a problem that long-term storage cannot be performed and proper concentration control is difficult.
【0012】また従来の電解殺菌法では、一般的に白金
や二酸化ルテニウム等の金属材料や黒鉛等が使われてい
るが、前記廃液処理と同様に、腐食や摩耗の問題があ
る。Further, in the conventional electrolytic sterilization method, a metal material such as platinum or ruthenium dioxide, graphite, or the like is generally used, but there is a problem of corrosion and abrasion as in the waste liquid treatment.
【0013】本発明の目的は、廃液処理、浄水生成およ
び電解水生成等の各種水処理方法において、上記のよう
な諸問題のない、固体活性炭の、触媒作用、吸着能力、
電流密度大で低抵抗の固体電極材料である等の特性を生
かした、短時間で効果的に電解酸化することのできる、
優れた電解酸化水処理方法を提供することにある。[0013] It is an object of the present invention to provide various water treatment methods such as waste liquid treatment, purified water generation, and electrolyzed water generation, which are free from the above-mentioned problems and have a catalytic action, adsorption ability, and the like of solid activated carbon.
Utilizing characteristics such as a solid electrode material with high current density and low resistance, it is possible to perform electrolytic oxidation effectively in a short time,
An object of the present invention is to provide an excellent electrolytic oxidation water treatment method.
【0014】[0014]
【課題を解決するための手段】上記の課題・目的は以下
に示す本発明によって解決・達成される。The above objects and objects are solved and achieved by the present invention described below.
【0015】すなわち、本発明は、電解酸化により水処
理する方法において、電解用電極が活性炭/炭素複合材
料よりなる固体活性炭電極であり、且つ前記活性炭が活
性炭粉末または活性炭繊維よりなり、前記炭素複合材料
がフェノール樹脂の炭化物の複合材料である固体活性炭
電極を、陰極または陽極の少なくとも一方に具備してな
る電気分解槽を用い、被処理水を電解酸化分解処理する
ことを特徴とする電解酸化水処理方法を開示するもので
ある。That is, according to the present invention, in the method for water treatment by electrolytic oxidation, the electrode for electrolysis is a solid activated carbon electrode made of activated carbon / carbon composite material, and the activated carbon is made of activated carbon powder or activated carbon fiber; Electrolytic oxidizing water characterized by subjecting water to be treated to electrolytic oxidative decomposition using an electrolysis tank provided with a solid activated carbon electrode, which is a composite material of a phenolic carbide, at least one of a cathode and an anode. It discloses a processing method.
【0016】また、本発明は、前記被処理水が産業廃液
であり、該産業廃液を電解酸化分解処理する廃液処理方
法であることを特徴とするするものであり、さらには該
産業廃液が、めっき液等金属イオンを含む廃液であるこ
とを特徴とするするものである。Further, the present invention is characterized in that the water to be treated is an industrial waste liquid and is a waste liquid treatment method for subjecting the industrial waste liquid to electrolytic oxidative decomposition treatment. It is a waste liquid containing metal ions such as a plating solution.
【0017】また、本発明は、前記被処理水が水道水で
あり、該水道水を電解酸化分解浄化処理する浄水生成方
法であり、且つ浄化後固体活性炭への付着物を電気分解
により処理する機構を具備してなることを特徴とするも
のである。The present invention is also a method for producing purified water, wherein the water to be treated is tap water, and the tap water is subjected to electrolytic oxidative decomposition purification treatment, and after purification, deposits on solid activated carbon are treated by electrolysis. It is characterized by comprising a mechanism.
【0018】また、本発明は、前記被処理水が水であ
り、該水を電気分解させて電解水を得る電解水生成方法
であるであることを特徴とするするものである。Further, the present invention is characterized in that the water to be treated is water, and the method is a method for producing electrolyzed water by electrolyzing the water to obtain electrolyzed water.
【0019】本発明における固体活性炭は、通常の活性
炭粉末をフェノール樹脂の炭化物で結合させてなる固体
状の活性炭である。したがって、表面積が非常に大き
く、触媒作用があり、吸着能力に優れる等の、活性炭が
有する本来の優れた特性をそのまま維持しつつ、加えて
低抵抗で密度が高く、取り扱いの容易な優れた固体状の
電極が実現することとなった。The solid activated carbon in the present invention is a solid activated carbon obtained by binding ordinary activated carbon powder with a phenolic carbide. Therefore, while maintaining the original excellent properties of activated carbon, such as a very large surface area, having a catalytic action, and excellent adsorption capacity, it is also an excellent solid that has low resistance, high density, and easy handling. Electrode is realized.
【0020】その結果、上記の固体活性炭を電解電極に
用いることにより、効率的で安価な酸化電解装置を構成
することができ、廃液処理、浄水生成および電解水生成
等の優れた各種の電解酸化水処理方法を提供することが
可能となった。As a result, by using the above-mentioned solid activated carbon for the electrolytic electrode, an efficient and inexpensive oxidizing electrolyzer can be constructed, and various kinds of excellent electrolytic oxidizing processes such as waste liquid treatment, purified water generation and electrolyzed water generation can be achieved. It has become possible to provide a water treatment method.
【0021】[0021]
【発明の実施の形態】以下、図面を参照して本発明の実
施態様を説明する。Embodiments of the present invention will be described below with reference to the drawings.
【0022】[0022]
【実施例】図面に基づいて実施例により本発明を詳細に
説明するが、本発明がこれらによって何ら限定されるも
のではない。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail with reference to embodiments based on the drawings, but the present invention is not limited thereto.
【0023】[実施例1]実施例1として、活性炭粉末
70重量%と、フェノール樹脂30重量%を混合した粉
末を0.5tonf/cm2のプレス圧力で成型した。得
られた活性炭含有フェノール樹脂の成型体を電気炉中、
N2雰囲気下に900℃で2時間熱処理を行った。熱処
理によって、フェノール樹脂が炭化された結果、活性炭
/炭素複合体である固体活性炭が得られた。Example 1 As Example 1, a powder obtained by mixing 70% by weight of activated carbon powder and 30% by weight of a phenol resin was molded at a pressing pressure of 0.5 tonf / cm 2. The obtained activated carbon-containing phenolic resin molded body in an electric furnace,
Heat treatment was performed at 900 ° C. for 2 hours in an N 2 atmosphere. As a result of the heat treatment, the phenol resin was carbonized, and as a result, solid activated carbon, which was an activated carbon / carbon composite, was obtained.
【0024】得られた固体活性炭は、比表面積800m
2/g、密度0.9g/cm3、大きさ15×10×0.3
cmである。こうして得られた固体活性炭電極1を1
対、電解槽2に設置し、電解槽2には廃液を満たした。
廃液は、COD値が500mg/lで中性の界面活性剤
を溶かしたものである。廃液には、さらに0.5g/l
の塩化ナトリウムを加えた。The obtained solid activated carbon has a specific surface area of 800 m.
2 / g, density 0.9 g / cm 3, size 15 × 10 × 0.3
cm. The solid activated carbon electrode 1 thus obtained was
On the other hand, it was installed in the electrolytic cell 2 and the electrolytic cell 2 was filled with waste liquid.
The waste liquid has a COD value of 500 mg / l and a neutral surfactant dissolved therein. The waste liquid further contains 0.5 g / l
Of sodium chloride was added.
【0025】固体活性炭電極1間に直流電源3により、
10Vで100Aの定電流を10分間流した。このよう
な電解酸化を行った後の廃液のCOD値は18mg/l
まで低下した。A DC power supply 3 is provided between the solid activated carbon electrodes 1 to
A constant current of 100 A was applied at 10 V for 10 minutes. The COD value of the waste liquid after performing such electrolytic oxidation is 18 mg / l.
Down to
【0026】[実施例2]実施例2として、実施例1と
同様の構成により、銅イオンの5g/lを含み、0.5
g/lの塩化ナトリウムを加えた廃液に、実施例1と同
様の電解酸化を行った。電解酸化後の廃液の銅イオン濃
度は、2mg/lまで低下した。[Embodiment 2] As Embodiment 2, the same configuration as that of Embodiment 1 is used, containing 5 g / l of copper ion and 0.5.
The same electrolytic oxidation as in Example 1 was performed on the waste liquid to which g / l of sodium chloride had been added. The copper ion concentration of the waste liquid after the electrolytic oxidation was reduced to 2 mg / l.
【0027】[実施例3]実施例3として、実施例1と
同様の方法により作製した一対の固体活性炭電極1を、
トリクロロメタン濃度50ppbの水道水に浸した。水
道水を十分攪拌した後のトリクロロメタン濃度は1pp
bに減少した。このバッチ処理を1日1回30日間行っ
た。その際、固体活性炭電極1間に10Vで100Aの
定電流を流した場合には、流さなかった場合に比べて、
細菌の数を5%に抑えることができた。Example 3 As Example 3, a pair of solid activated carbon electrodes 1 manufactured by the same method as in Example 1 was used.
It was immersed in tap water having a trichloromethane concentration of 50 ppb. The trichloromethane concentration after sufficiently stirring the tap water is 1 pp
b. This batch process was performed once a day for 30 days. At that time, when a constant current of 100 A was flowed between the solid activated carbon electrodes 1 at 10 V, compared with a case where no current was flowed,
The number of bacteria could be reduced to 5%.
【0028】[実施例4]実施例4として、実施例1と
同様の方法により固体活性炭を作製した。電解室4は隔
膜5を有しており、二個の電解室に仕切られている。各
電解室に固体活性炭電極1を設置し、それぞれ直流電源
3の陽極端子および陰極端子に接続した。電解室4に塩
化ナトリウムを0.5g/lの割合で溶かした水道水を
満たした。Example 4 As Example 4, a solid activated carbon was produced in the same manner as in Example 1. The electrolytic chamber 4 has a diaphragm 5 and is divided into two electrolytic chambers. The solid activated carbon electrode 1 was installed in each electrolytic chamber, and connected to the anode terminal and the cathode terminal of the DC power supply 3, respectively. The electrolytic chamber 4 was filled with tap water in which sodium chloride was dissolved at a rate of 0.5 g / l.
【0029】固体活性炭電極1間に、10Vで100A
の直流電流を10分間流した。100 A at 10 V between solid activated carbon electrodes 1
For 10 minutes.
【0030】その後、陽極端子に接続された固体活性炭
電極1が設けられた電解室4に、蛋白性の汚れを塗布し
たガラス板6を浸漬した結果、約5分後にはこのタンパ
ク質が分解された。Thereafter, the glass plate 6 coated with proteinaceous soil was immersed in the electrolytic chamber 4 provided with the solid activated carbon electrode 1 connected to the anode terminal. As a result, the protein was decomposed after about 5 minutes. .
【0031】[比較例1]次に比較例1として、大きさ
は15×10×0.3cmである黒鉛板を電極に用い
て、実施例1と同様の廃液処理を行った。実施例1と同
様の電流密度の10Vで100Aを流すと、陽極が瞬時
に摩耗してしまった。そこで、黒鉛板の摩耗が激しく起
こらない0.1Aの定電流を10分間流した。その結
果、廃液のCOD値は250mg/lまでしか下がらな
かった。Comparative Example 1 Next, as Comparative Example 1, the same waste liquid treatment as in Example 1 was performed using a graphite plate having a size of 15 × 10 × 0.3 cm as an electrode. When 100 A was passed at a current density of 10 V similar to that in Example 1, the anode was instantaneously worn. Therefore, a constant current of 0.1 A, which does not cause abrasion of the graphite plate, was applied for 10 minutes. As a result, the COD value of the waste liquid decreased only to 250 mg / l.
【0032】[0032]
【発明の効果】上記のように、本発明の電解酸化水処理
方法は、固体活性炭よりなる電解電極を有する電解槽を
用いて電解酸化することにより、電流密度を非常に大き
くすることができるため、短時間で効果的に電解酸化す
ることができるという効果を発揮する。As described above, according to the electrolytic oxidizing water treatment method of the present invention, the current density can be greatly increased by performing electrolytic oxidation using an electrolytic cell having an electrolytic electrode made of solid activated carbon. The effect is that the electrolytic oxidation can be performed effectively in a short time.
【0033】さらに、活性炭の触媒作用、高吸着能力、
低抵抗の電極材料としての優れた特性を生かして、廃液
処理、浄水生成および電解水生成等の電解酸化による水
処理に関するあらゆる装置に応用することができ、顕著
な効果が奏される。Further, the catalytic action of activated carbon, high adsorption capacity,
Taking advantage of the excellent characteristics as a low-resistance electrode material, it can be applied to all devices related to water treatment by electrolytic oxidation such as waste liquid treatment, purified water generation, and electrolytic water generation, and has a remarkable effect.
【図1】本発明の一実施例の電解酸化水処理を行う装置
の構成を示す模式図。FIG. 1 is a schematic view showing a configuration of an apparatus for performing electrolytic oxidized water treatment according to one embodiment of the present invention.
【図2】本発明の他の実施例の電解酸化水処理を行う装
置の構成を示す模式図。FIG. 2 is a schematic view showing a configuration of an apparatus for performing electrolytic oxidized water treatment according to another embodiment of the present invention.
1 固体活性炭電極 2 電解槽 3 直流電源 4 電解室 5 隔壁 6 蛋白質を塗布したガラス板 DESCRIPTION OF SYMBOLS 1 Solid activated carbon electrode 2 Electrolyzer 3 DC power supply 4 Electrolysis chamber 5 Partition wall 6 Glass plate which applied protein
Claims (5)
て、電解用電極が活性炭/炭素複合材料よりなる固体活
性炭電極であり、且つ前記活性炭が活性炭粉末または活
性炭繊維よりなり、前記炭素複合材料がフェノール樹脂
の炭化物の複合材料である固体活性炭電極を、陰極また
は陽極の少なくとも一方に具備してなる電気分解槽を用
い、被処理水を電解酸化分解処理することを特徴とする
電解酸化水処理方法。1. A method for treating water by electrolytic oxidation, wherein the electrode for electrolysis is a solid activated carbon electrode made of an activated carbon / carbon composite material, and the activated carbon is made of activated carbon powder or activated carbon fiber, and the carbon composite material is a phenol resin. A process for electrolytically oxidizing and decomposing water to be treated using an electrolysis tank provided with at least one of a cathode and an anode, which is a solid activated carbon electrode which is a composite material of carbides.
法が、産業廃液を電解酸化分解処理する廃液処理方法で
ある請求項1記載の電解酸化水処理方法。2. The electrolytic oxidized water treatment method according to claim 1, wherein the method for electrolytically decomposing the water to be treated is a waste liquid treatment method for electrolytically oxidizing and decomposing industrial waste liquid.
を含む廃液である請求項2記載の電解酸化水処理方法。3. The electrolytic oxidized water treatment method according to claim 2, wherein the industrial waste liquid is a waste liquid containing metal ions such as a plating solution.
法が、水道水の電解酸化分解浄化処理を行う浄水生成方
法であり、且つ浄化後固体活性炭への付着物を電気分解
により処理する機構を具備してなることを特徴とする請
求項1記載の電解酸化水処理方法。4. The method for electrolytically oxidizing and decomposing water to be treated is a purified water producing method for performing electrolytic oxidatively decomposing and purifying treatment of tap water, and a mechanism for treating the deposits on the solid activated carbon after purification by electrolysis. The method for treating electrolytic oxidized water according to claim 1, comprising:
法が、水を電気分解させて電解水を得る電解水生成方法
である請求項1記載の電解酸化水処理方法。5. The electrolytic oxidized water treatment method according to claim 1, wherein the method of electrolytically decomposing the water to be treated is an electrolytic water generation method of electrolyzing water to obtain electrolytic water.
Priority Applications (1)
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JP16469197A JPH1110160A (en) | 1997-06-20 | 1997-06-20 | Method for treating water by electrolytic oxidation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16469197A JPH1110160A (en) | 1997-06-20 | 1997-06-20 | Method for treating water by electrolytic oxidation |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH1110160A true JPH1110160A (en) | 1999-01-19 |
Family
ID=15798037
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16469197A Pending JPH1110160A (en) | 1997-06-20 | 1997-06-20 | Method for treating water by electrolytic oxidation |
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JP (1) | JPH1110160A (en) |
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WO2012114999A1 (en) * | 2011-02-21 | 2012-08-30 | 東洋炭素株式会社 | Organic acid-containing liquid degradative treatment method, organic acid-containing liquid degradative treatment device, and electrode for organic acid-containing liquid degradative treatment |
JP2013052383A (en) * | 2011-09-05 | 2013-03-21 | Yoshiko Moriyasu | Device and method for purifying water |
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1997
- 1997-06-20 JP JP16469197A patent/JPH1110160A/en active Pending
Cited By (7)
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WO2012114999A1 (en) * | 2011-02-21 | 2012-08-30 | 東洋炭素株式会社 | Organic acid-containing liquid degradative treatment method, organic acid-containing liquid degradative treatment device, and electrode for organic acid-containing liquid degradative treatment |
JP2013052383A (en) * | 2011-09-05 | 2013-03-21 | Yoshiko Moriyasu | Device and method for purifying water |
CN103721746A (en) * | 2012-10-12 | 2014-04-16 | 中国石油化工股份有限公司 | Composite catalyst used for industrial wastewater treatment via electrolytic oxidation, and preparation method thereof |
CN104341027A (en) * | 2013-07-25 | 2015-02-11 | 常州市排水管理处 | Efficient decolorization and dephosphorization filler, its preparation method, and decolorization and dephosphorization method |
CN103691417A (en) * | 2013-12-24 | 2014-04-02 | 南京大学 | Preparation method of TiO2/ACF (Active Carbon Fiber) catalytic material and application thereof |
CN105000626A (en) * | 2015-06-26 | 2015-10-28 | 中山大学 | Method for reinforcing piezoelectric effect to improve organic pollutant degradation efficiency and application thereof |
CN105198048A (en) * | 2015-10-27 | 2015-12-30 | 雅本化学股份有限公司 | Three-dimensional electrode filling material and preparation method thereof |
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