JPH0913185A - Production of hydrogen peroxide and water tank - Google Patents

Production of hydrogen peroxide and water tank

Info

Publication number
JPH0913185A
JPH0913185A JP7161951A JP16195195A JPH0913185A JP H0913185 A JPH0913185 A JP H0913185A JP 7161951 A JP7161951 A JP 7161951A JP 16195195 A JP16195195 A JP 16195195A JP H0913185 A JPH0913185 A JP H0913185A
Authority
JP
Japan
Prior art keywords
water
oxygen
cathode
water tank
air
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
JP7161951A
Other languages
Japanese (ja)
Inventor
Tamotsu Kodera
保 小寺
Yoshikazu Sakakibara
嘉一 榊原
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.)
Takuma Co Ltd
Original Assignee
Takuma 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 Takuma Co Ltd filed Critical Takuma Co Ltd
Priority to JP7161951A priority Critical patent/JPH0913185A/en
Publication of JPH0913185A publication Critical patent/JPH0913185A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C02F1/4672Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
    • C02F1/4674Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation with halogen or compound of halogens, e.g. chlorine, bromine
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/78Treatment of water, waste water, or sewage by oxidation with ozone
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/04Disinfection

Abstract

PURPOSE: To easily and effectively disinfect the water stored in various tanks. CONSTITUTION: An electrolytic cell 2 with the gas diffusing electrode 5 provided with an oxygen-contg. gas passage 7 on its rear as a cathode and an air-lift pump 3 are inserted into the water, the oxygen-contg. gas passed through the cell is introduced into the air-lift pump, and the water in the electrolytic compartment 6 of the cell is sucked by the resultant suction force. The distance between an anode 4 and the cathode 5 is preferably controlled to 0.2-5mm to treat the water having about the same conductivity as city water. The disinfected water is safe for other organisms such as fishes, the environment is not polluted, the structure of the equipment is made compact, and the running cost is reduced. Further, the installation and maintenance are simplified, liq. chemicals, etc., need not be replenished, and this type of water tank is economically and easily utilized as a large industrial water tank as well as the water tank for goldfishes and tropical fishes.

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、電解セルとリフト管と
を用いた過酸化水素の製造方法および水槽に関し、魚類
の飼育水槽、プール、工業用水槽などの水の消毒に広く
利用することができる。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing hydrogen peroxide using an electrolysis cell and a lift tube and a water tank, which can be widely used for disinfecting water in fish breeding water tanks, pools, industrial water tanks and the like. You can

【0002】[0002]

【従来の技術】水槽などの水の消毒には、古くから塩
素、次亜塩素酸ナトリウム、二酸化塩素などの薬液注
入、紫外線照射、ろ過などの各種方法が、目的に応じて
単独または組合せて利用されている。しかし、塩素系薬
剤を使用すればトリハロメタンの前駆物質の生成のおそ
れがあり、好ましいとは言えない。紫外線照射による消
毒は、処理水の透明度に影響されやすく、水中の紫外線
透過率があまり大きくないので、水槽全体を有効に消毒
するには紫外線ランプが多数必要になり、経済的負担が
大きい。
2. Description of the Related Art For the disinfection of water in water tanks, various methods such as injection of chemicals such as chlorine, sodium hypochlorite, chlorine dioxide, ultraviolet irradiation and filtration have been used singly or in combination depending on the purpose. Has been done. However, the use of chlorine-based chemicals is not preferable because there is a risk of generation of trihalomethane precursors. The disinfection by ultraviolet irradiation is easily affected by the transparency of the treated water, and the ultraviolet transmittance in water is not so large. Therefore, a large number of ultraviolet lamps are required to effectively disinfect the whole water tank, which imposes a heavy financial burden.

【0003】[0003]

【発明が解決しようとする課題】そこで、本発明は、各
種水槽の貯留水を簡易かつ効果的に消毒する方法と消毒
容易な水槽とを提供する目的で完成されてのである。本
発明において、水槽は、各種の魚類飼育用水槽、飲料水
用水槽、産業用水槽、防火水槽などのほかにプールや養
魚場などを含むものである。
Therefore, the present invention has been completed for the purpose of providing a method for easily and effectively disinfecting stored water in various water tanks and a water tank for easy disinfection. In the present invention, the water tank includes various fish breeding water tanks, drinking water water tanks, industrial water tanks, fire prevention water tanks, and the like, as well as pools and fish farms.

【0004】[0004]

【課題を解決するための手段】図1を参照して説明す
る。本発明は、酸素含有気体の流路7が裏面側に設けら
れているガス拡散電極5を陰極とする電解セル2とエア
リフト管3とを水中に挿入し、電解セルを通過する酸素
含有気体をエアリフト管に導入して電解セルの電解室6
の水を吸引させることを特徴とする過酸化水素の製造方
法を提供する。最も一般的な水道水や工業用水程度の電
気伝導度を有する水を処理するには、陽極と陰極との間
隔Aを0.2〜5mmとすることが好ましい。
A description will be given with reference to FIG. The present invention inserts an electrolysis cell 2 having a gas diffusion electrode 5 having a flow path 7 for oxygen-containing gas on the back surface side as a cathode and an air lift tube 3 into water to remove an oxygen-containing gas passing through the electrolysis cell. Electrolyte chamber 6 of electrolysis cell introduced into air lift tube
And a method for producing hydrogen peroxide, which comprises sucking the water. In order to treat the most common tap water or water having an electric conductivity of about industrial water, the distance A between the anode and the cathode is preferably 0.2 to 5 mm.

【0005】また、本発明は、裏面側に酸素含有気体の
流路7が設けられているガス拡散電極の陰極5と、電解
室6を挾んで陰極に対峙する陽極4とから構成されてい
る電解セル2、ならびに電解セルを通過した酸素含有気
体を気体源にするエアリフト管3が設けられ、陰極裏面
に吹込んだ酸素含有気体をエアリフト管底部に導き、電
解室6の水をエアリフト管により吸引せしめていること
を特徴とする水槽水槽1を提供する。
Further, the present invention is composed of a cathode 5 of a gas diffusion electrode having a flow path 7 for oxygen-containing gas on the back side thereof, and an anode 4 which faces the cathode by sandwiching the electrolysis chamber 6. An electrolysis cell 2 and an air lift pipe 3 that uses the oxygen-containing gas that has passed through the electrolysis cell as a gas source are provided. Provided is an aquarium tank 1 characterized by being sucked.

【0006】[0006]

【作用と実施態様例】本発明を図1を参照して実施態様
例をあげつつ、具体的に説明する。図1は本発明の実施
態様例を示す模式図である。本発明を用いて過酸化水素
を製造し、例えば水槽内の水を消毒するには、水槽1内
に陽極4と電解室6を挟んで電解室6陽極に対峙するガ
ス拡散電極の陰極5とから構成される電解セル2とエア
リフト管3とを取り付ける。電解室6とエアリフト管3
の下部側面との間には、例えば導水管8を設けて電解室
6内の水がエアリフト管3により効果的に吸引されるよ
うにする。電極材料としては、陽極には陽イオンを生成
しない材料としてチタンにイリジウムや白金をコーティ
ングしたもの、陰極はカーボンブラックを主体にポリテ
トラフルオロエチレン(PTFE)の粉末などを練合わ
せて成形したものがよい。陰極5の裏面側には酸素含有
気体の流路7を設ける。酸素含有気体に空気を使用する
場合を例にあげると、エアポンプ9などにより空気送入
管10を経て空気を送入できるようにする。流路7の出
口側とエアリフト管3の底部との間には、例えば気体導
管11を設けてエアリフト管3への気体の送入を容易に
しておく。
Actions and Embodiments The present invention will be specifically described with reference to FIG. FIG. 1 is a schematic view showing an embodiment example of the present invention. In order to produce hydrogen peroxide using the present invention, for example, to disinfect water in a water tank, a cathode 5 of a gas diffusion electrode that faces the anode of the electrolytic chamber 6 with the anode 4 and the electrolytic chamber 6 sandwiched in the water tank 1 is used. The electrolysis cell 2 and the air lift tube 3 are attached. Electrolysis chamber 6 and air lift tube 3
A water guide pipe 8 is provided, for example, between the lower side surface and the lower side face so that the water in the electrolysis chamber 6 is effectively sucked by the air lift pipe 3. As the electrode material, the anode is one in which titanium is coated with iridium or platinum as a material that does not generate cations, and the cathode is one in which carbon black is mainly mixed and powder of polytetrafluoroethylene (PTFE) is kneaded and molded. Good. A flow path 7 for oxygen-containing gas is provided on the back surface side of the cathode 5. Taking the case where air is used as the oxygen-containing gas, for example, the air can be fed through the air feed pipe 10 by the air pump 9 or the like. A gas conduit 11, for example, is provided between the outlet side of the flow path 7 and the bottom of the air lift pipe 3 to facilitate the introduction of gas into the air lift pipe 3.

【0007】さて、エアポンプ9により流路7に送入さ
れた空気は、さらにエアリフト管3に導かれ、底部から
上向きに流れ、水と混相流を形成してエアリフト作用を
奏する。このエアリフト作用により電解室6内の水が吸
引され、水槽1内の水が電解室6に吸引される。この
間、電解室6においては電解還元が行われ、酸素が還元
されて過酸化水素が製造される。水と気体とはエアリフ
ト管上部から排出され、水は製造した過酸化水素ととも
に水槽へ戻される。水槽内の水は過酸化水素により消毒
され、清浄状態を維持することができる。電解セルに
は、電源12からリード線13を経て電気が供給され
る。処理水は、電気分解の容易性の点からは導電性の高
い電解質を多く含んだものが望ましいが、一般的に使用
される水道水のように100〜300μS/cm程度の
導電性を有する水でも、陽極と陰極との間隔を0.2〜
5mm程度にすることにより、低電圧で無理なく本発明
を実施することが可能になる。なお、電解セルは水中に
浸漬するので、電解セルその他の絶縁性に十分留意する
必要がある。
The air sent into the flow path 7 by the air pump 9 is further guided to the air lift pipe 3 and flows upward from the bottom portion to form a multiphase flow with water, thereby exhibiting an air lift action. Water in the electrolysis chamber 6 is sucked by this air lift action, and water in the water tank 1 is sucked in the electrolysis chamber 6. During this period, electrolytic reduction is performed in the electrolytic chamber 6 to reduce oxygen and produce hydrogen peroxide. Water and gas are discharged from the upper part of the air lift pipe, and the water is returned to the water tank together with the produced hydrogen peroxide. The water in the water tank is disinfected with hydrogen peroxide and can be kept in a clean state. Electricity is supplied to the electrolysis cell from a power supply 12 via a lead wire 13. From the viewpoint of ease of electrolysis, the treated water preferably contains a large amount of highly conductive electrolyte, but water having a conductivity of about 100 to 300 μS / cm, such as commonly used tap water. However, the distance between the anode and the cathode is 0.2 ~
By setting the thickness to about 5 mm, the present invention can be easily implemented at a low voltage. Since the electrolytic cell is immersed in water, it is necessary to pay sufficient attention to the insulating properties of the electrolytic cell and the like.

【0008】本発明に使用する酸素含有気体としては一
般的には経済的な空気を用いるが、規模の大きな水槽で
過酸化水素の生成効率を高めたいときなどは、空気より
も酸素濃度の高い気体、例えば、PSA式酸素発生機で
空気を処理した酸素濃度90〜95%の酸素含有気体、
ボンベ入り酸素などを使用することができる。また、電
解セルへ吸入する水量調整は、電解室またはエアリフト
管への酸素含有気体の流量調節により行うことができ
る。水量が多くなれば、電解セルを出た水中の過酸化水
素の濃度は低くなるが、生成される過酸化水素量は水量
の増減にかかわらずほぼ一定である。
Generally, economical air is used as the oxygen-containing gas used in the present invention, but when the production efficiency of hydrogen peroxide is desired to be increased in a large-scale water tank, the oxygen concentration is higher than that of air. A gas, for example, an oxygen-containing gas having an oxygen concentration of 90 to 95% obtained by treating air with a PSA oxygen generator,
Oxygen in a cylinder can be used. The amount of water sucked into the electrolytic cell can be adjusted by adjusting the flow rate of the oxygen-containing gas to the electrolytic chamber or the air lift pipe. When the amount of water increases, the concentration of hydrogen peroxide in the water discharged from the electrolysis cell decreases, but the amount of hydrogen peroxide produced is almost constant regardless of the increase or decrease in the amount of water.

【0009】[0009]

【実施例】本発明の効果を確認するために、電極間距離
を変えた過酸化水素の発生実験とエアリフト管の揚水実
験とを実施したのでその結果を示す。 実施例 1 陽極にチタンをベースとして酸化イリジウムをコーティ
ングした電極を、陰極にカーボンブラックとポリテトラ
フロロエチレンの粉末を混合して成形したガス拡散電極
を用い、電極面積0.18dm2 の電解セルで、水道水
を電解液とし、酸素含有気体として空気を用いて電解還
元を実施し、過酸化水素の発生を確認した。電解条件
は、空気量500ml/min、水道水量100〜33
0ml/min(16.3℃)、電極間電圧5.04V
であった。水量は電解セル出口の過酸化水素生成水をメ
スシリンダーに受けて実測し、過酸化水素濃度は過マン
ガン酸カリ法により測定した。測定結果を表1に示す。
EXAMPLE In order to confirm the effect of the present invention, a hydrogen peroxide generation experiment with a different distance between electrodes and a pumping experiment of an air lift pipe were carried out. The results are shown. Example 1 An electrolytic cell having an electrode area of 0.18 dm 2 was prepared by using an electrode having an anode coated with iridium oxide based on titanium, and a cathode having a gas diffusion electrode formed by mixing carbon black and polytetrafluoroethylene powder. The generation of hydrogen peroxide was confirmed by performing electrolytic reduction using tap water as an electrolytic solution and air as an oxygen-containing gas. The electrolysis conditions are an air amount of 500 ml / min and a tap water amount of 100 to 33.
0 ml / min (16.3 ° C), voltage between electrodes 5.04V
Met. The amount of water was measured by receiving hydrogen peroxide-forming water at the outlet of the electrolysis cell in a measuring cylinder, and the hydrogen peroxide concentration was measured by the potassium permanganate method. Table 1 shows the measurement results.

【0010】[0010]

【表1】 電極間距離 水 量 電 流 値 過酸化水素濃度 mm ml/min A ppm 0.5 330 0.24 7 1 330 0.15 4 5 330 0.04 1 0.5 100 0.24 23 実施例 2 図2に概要を示した装置を用い、水槽21内に、陽極2
4とガス拡散電極である陰極25との間に電解室26が
設けられている電解セル22およびエアリフト管23を
取り付け、電解セルに送入する空気量を変化させて揚水
量をはかり、エアリフト管の性能を確認した。エアリフ
ト管の有効長が160mm、導水管28、気体送入管3
0および気体導管31には内径5mm、外径8mmのシ
リコン管を用いた。電解セルの電極面積は18cm2
電極間の距離は0.5mmであった。エアリフト管から
の揚水量は、揚水排出管32から溢流する水をメスフラ
スコ33に受けて測定した。
[Table 1] Distance between electrodes Water amount Current value Hydrogen peroxide concentration mm ml / min A ppm 0.5 330 330 0.24 7 1 330 330 0.15 4 5 330 0.04 1 0.5 100 100 0.24 23 Example 2 The anode 2 was placed in a water tank 21 using the apparatus outlined in FIG.
4 and a cathode 25 which is a gas diffusion electrode, an electrolysis cell 22 having an electrolysis chamber 26 and an air lift pipe 23 are attached, and the amount of pumped water is changed by changing the amount of air sent into the electrolysis cell. Confirmed the performance of. The effective length of the air lift pipe is 160 mm, the water conduit 28, the gas inlet pipe 3
A silicon tube having an inner diameter of 5 mm and an outer diameter of 8 mm was used for 0 and the gas conduit 31. The electrode area of the electrolysis cell is 18 cm 2 ,
The distance between the electrodes was 0.5 mm. The amount of pumped water from the air lift pipe was measured by receiving the water overflowing from the pumped water discharge pipe 32 in the measuring flask 33.

【0011】[0011]

【表2】 空気量(ml/min) 揚水量(ml/min) 660 70 800 90 1,300 120 2,500 140[Table 2] Air volume (ml / min) Pumped water volume (ml / min) 660 70 800 90 90 1,300 120 2,500 140

【0012】[0012]

【発明の効果】本発明の過酸化水素製造方法は、水槽な
どの水の消毒用に手軽に利用することができる。塩素系
殺菌剤のようにトリハロメタン前駆物質を生成する懸念
はなく、また、水酸化ナトリウムなどの第3物質を使用
しないので、消毒された水は魚類などの他の生物に安全
であり環境汚染の懸念もない。一般に使用される導電性
の低い水道水や工業用水でも、電極間距離を狭くするこ
とにより、高電圧を必要としないで過酸化水素を発生し
て消毒することができる。電解セルの水は、陰極に使用
した酸素含有気体の排気を利用するエアリフトにより吸
引して供給するので、コストがかからない上、水ポンプ
設置の必要がなく、全体の機器構成がコンパクトになり
運転経費を節約できる効果がある。通常、酸素含有気体
に、通常、空気を用いるので、送入空気量を増減し水の
送入量を容易に調整することができる。大きな水槽の水
を消毒する場合などで、過酸化水素発生量を増大する必
要がある場合には、酸素含有気体中の酸素濃度を高めれ
ば、機器を大きくすることなく対応することができる。
設置と保全が簡単で薬液などの補充を要せず、金魚、熱
帯魚の水槽から大きな工業用水槽に経済的に容易に利用
できる。
The method for producing hydrogen peroxide of the present invention can be easily used for disinfecting water in a water tank or the like. There is no concern about producing trihalomethane precursors like chlorine-based bactericides, and since no third substance such as sodium hydroxide is used, disinfected water is safe for other organisms such as fish and causes no environmental pollution. There is no concern. Even in tap water or industrial water, which is generally used and has low conductivity, hydrogen peroxide can be generated and disinfected without requiring a high voltage by reducing the distance between the electrodes. The water in the electrolysis cell is sucked and supplied by an air lift that uses the exhaust of the oxygen-containing gas used for the cathode, so there is no cost, there is no need to install a water pump, and the overall equipment configuration is compact and operating costs are high. There is an effect that can be saved. Since air is usually used as the oxygen-containing gas, it is possible to easily adjust the amount of supplied air by increasing or decreasing the amount of supplied air. When it is necessary to increase the amount of hydrogen peroxide generated, such as when disinfecting water in a large water tank, increasing the oxygen concentration in the oxygen-containing gas can cope with this without increasing the size of the equipment.
It is easy to install and maintain, does not require replenishment of chemicals, etc., and can be economically used easily from aquariums of goldfish and tropical fish to large industrial aquariums.

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

【図1】本発明の実施態様例を示す模式図。FIG. 1 is a schematic diagram showing an example of an embodiment of the present invention.

【図2】実施例2に用いた試験装置の模式図。FIG. 2 is a schematic diagram of a test apparatus used in Example 2.

【符号の説明】[Explanation of symbols]

1:水槽 2:電解セル 3:エアリフト管 4:陽極 5:陰極 6:電解室 7:酸素含有
気体の流路 8:導水管 9:エアポンプ 10:気体送入管
11:気体導管 12:電源 13:リード線 21:水槽 22:電解セル 23:エアリフト管
24:陽極 25:陰極 26:電解室 27:酸素含有気体の
流路 28:導水管 29:エアポンプ 30:気体送入
管 31:気体導管 32:揚水排出管 33:メスフ
ラスコ
1: Water tank 2: Electrolysis cell 3: Air lift pipe 4: Anode 5: Cathode 6: Electrolysis chamber 7: Oxygen-containing gas passage 8: Water conduit 9: Air pump 10: Gas inlet pipe
11: Gas conduit 12: Power supply 13: Lead wire 21: Water tank 22: Electrolysis cell 23: Air lift pipe 24: Anode 25: Cathode 26: Electrolysis chamber 27: Oxygen-containing gas flow path 28: Water pipe 29: Air pump 30: Gas Inlet pipe 31: Gas conduit 32: Pumped water discharge pipe 33: Volumetric flask

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】酸素含有気体の流路7が裏面側に設けられ
ているガス拡散電極5を陰極とする電解セル2とエアリ
フト管3とを水中に挿入し、電解セルを通過する酸素含
有気体をエアリフト管に導入して電解セルの電解室6の
水を吸引させることを特徴とする過酸化水素の製造方
法。
1. An oxygen-containing gas that passes through an electrolysis cell by inserting an electrolysis cell 2 having a gas diffusion electrode 5 provided on the back surface side of the oxygen-containing gas 5 as a cathode and an air lift tube 3 into the water, Is introduced into an air lift tube to suck water in the electrolysis chamber 6 of the electrolysis cell.
【請求項2】陽極と陰極との間隔を0.2〜5mmとす
ることを特徴とする請求項1記載の過酸化水素の製造方
法。
2. The method for producing hydrogen peroxide according to claim 1, wherein the distance between the anode and the cathode is 0.2 to 5 mm.
【請求項3】酸素含有気体の流路7が裏面側に設けられ
ているガス拡散電極の陰極5と、電解室6を挾んで陰極
に対峙する陽極4とから構成されている電解セル2、な
らびに電解セルを通過した酸素含有気体を気体源にする
エアリフト管3が設けられ、陰極裏面に吹込んだ酸素含
有気体をエアリフト管底部に導き、電解室6の水をエア
リフト管により吸引せしめていることを特徴とする水
槽。
3. An electrolysis cell 2 comprising a cathode 5 of a gas diffusion electrode having a flow path 7 for oxygen-containing gas provided on the back surface side thereof, and an anode 4 facing the cathode with the electrolysis chamber 6 interposed therebetween. In addition, an air lift pipe 3 is provided, which uses the oxygen-containing gas that has passed through the electrolysis cell as a gas source, guides the oxygen-containing gas blown to the back surface of the cathode to the bottom of the air lift pipe, and sucks water in the electrolysis chamber 6 by the air lift pipe. An aquarium characterized by that.
JP7161951A 1995-06-28 1995-06-28 Production of hydrogen peroxide and water tank Pending JPH0913185A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7161951A JPH0913185A (en) 1995-06-28 1995-06-28 Production of hydrogen peroxide and water tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7161951A JPH0913185A (en) 1995-06-28 1995-06-28 Production of hydrogen peroxide and water tank

Publications (1)

Publication Number Publication Date
JPH0913185A true JPH0913185A (en) 1997-01-14

Family

ID=15745160

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7161951A Pending JPH0913185A (en) 1995-06-28 1995-06-28 Production of hydrogen peroxide and water tank

Country Status (1)

Country Link
JP (1) JPH0913185A (en)

Similar Documents

Publication Publication Date Title
JP3612569B2 (en) Low concentration hypochlorous acid-containing strongly acidic sterilizing water, low concentration hypochlorous acid-containing strongly acidic sterilizing water generating method, generating device, and low concentration hypochlorous acid-containing strongly acidic sterilizing water generating and discharging device
CN107509678B (en) Aquaculture system
JP3988827B2 (en) Method and apparatus for producing negative and positive redox potential (ORP) water
JP3689541B2 (en) Seawater electrolyzer
JP5752399B2 (en) Seawater electrolysis apparatus, seawater electrolysis system and seawater electrolysis method
JP5791377B2 (en) Seawater electrolysis system and seawater electrolysis method
KR101268040B1 (en) Device for producing slightly weak acidic hypochlorous acid water
CN105734602B (en) The equipment for being used to prepare hypochloric acid water
CN104609532B (en) Method for removing PPCPs in treatment process of drinking water
US20010022273A1 (en) Electrochemical treatment of water and aqueous salt solutions
JPH0960931A (en) Ultrasonic wave humidifying and sterilizing device
JPH0290995A (en) Water treatment process and device using electrolytic ozone
CN1898162B (en) Electrolytic cell for treating contaminated water
CN1332890C (en) Electrolytic device and method for disinfecting water in a water supply system by means of the generation of active chlorine
CN205710945U (en) For preparing the equipment of hypochloric acid water
KR101065278B1 (en) Method and device of sterilizing seawater
JPH0913185A (en) Production of hydrogen peroxide and water tank
JP2019198820A (en) Method for producing slightly acidic aqueous hypochlorous acid, electrolytic cell unit and production device
JP6114335B2 (en) Seawater electrolysis system and seawater electrolysis method
US11203813B2 (en) Device comprising a channel, a cathode, an anode and a power source, and method for the production of chlorine dioxide
CN111517541A (en) Water treatment device
CN211035348U (en) Raw material supply device for acidic electrolyzed water generator
JP2002010724A (en) Method for decomposing ammonia in sea water and device therefor
JPH09279377A (en) Producing device of hydrogen peroxide and its production
JPH07246039A (en) Device for enriching oxygen for water tank