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JP2714662B2 - Method and apparatus for producing sterile water - Google Patents

Method and apparatus for producing sterile water

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Publication number
JP2714662B2
JP2714662B2 JP63051765A JP5176588A JP2714662B2 JP 2714662 B2 JP2714662 B2 JP 2714662B2 JP 63051765 A JP63051765 A JP 63051765A JP 5176588 A JP5176588 A JP 5176588A JP 2714662 B2 JP2714662 B2 JP 2714662B2
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Japan
Prior art keywords
water
cathode
anode
chamber
treated water
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JP63051765A
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Japanese (ja)
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JPH01228589A (en
Inventor
進 近藤
Original Assignee
進 近藤
三浦電子株式会社
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Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、食品加工用の水、水泳用プール水、建物内
に設置される上水用の貯水槽内の水および空調用クーラ
ーおよびクーラーボックスに使用するクーラー水等の無
菌または静菌状態での水処理が好ましい場合の無菌水の
製造方法及び装置に関するものである。
The present invention relates to water for food processing, pool water for swimming, water in a water storage tank installed in a building, a cooler for air conditioning, and a cooler. The present invention relates to a method and an apparatus for producing aseptic water in a case where sterile or bacteriostatic water treatment of cooler water or the like used in a box is preferable.

[従来の技術] 一般に水は食品加工水に始まり、水泳用プール水、飲
み水に至るまで、雑菌等の混入のない、中性の無菌水で
あることが望ましい。殊にこれらの一般水は、水道法等
の要請から、同法に合致する水は、中性であることが要
求され、しかも食品衛生指導等の要請から水を停滞させ
ることなく、流水状態で、しかも使用に望まれる流量で
大量の水が生成される設備であることが要求されてい
る。
[Prior Art] Generally, water is desirably neutral aseptic water free of various bacteria and the like, from food processing water to swimming pool water and drinking water. In particular, these general waters are required to be neutral in accordance with the requirements of the Water Supply Law, etc., and are required to be neutral under the requirements of food hygiene guidance. In addition, it is required that the facility generate a large amount of water at a flow rate desired for use.

[発明が解決しようとする課題] ところが、原水の電気電導度は地域によって異なって
おり、また同じ水道水でも朝、夕では変化するという事
態があり、電解水として生成水を安定した特定のPHとし
て得ることは困難であり、また安定した中性無菌水を生
成する事は困難であった。また、流水状態で簡易な単一
設備で、大量の中性無菌水の生成技術は実際問題として
困難を伴い、せいぜい化学薬剤等を投入して、水の殺菌
を行い無菌にする以外はなかった。
[Problems to be Solved by the Invention] However, the electric conductivity of raw water varies from region to region, and the same tap water may change in the morning and evening. And it was difficult to produce stable neutral sterile water. In addition, the technology for producing a large amount of neutral aseptic water in a simple single facility under flowing water conditions is difficult as a practical matter, and there has been no other way than to sterilize the water by injecting at most a chemical agent etc. .

本発明は、上記事情を考慮してなされたもので、常温
下において流水状態のまま、しかも簡易な設備で無菌に
できると共に中性化できる無菌水の製造方法及びその装
置を提供することを目的とする。
The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a method and apparatus for producing aseptic water that can be sterilized and neutralized with simple equipment while being in flowing water at room temperature. And

[課題を解決するための手段] 本発明は、上記目的を達成するために、陽極と陰極間
を隔膜で仕切って陽極室と陰極室とを形成した電解槽内
に、処理水を、陽極室に流して無菌水化したのち、陰極
室へ流して中和するようにした方法であり、また周面に
陽極の筒を有し中央に陰極が配置されると共にその間を
隔膜で仕切られた電解槽と、その電解槽の陽極室内に処
理水を供給する処理水供給手段と、陽極室内の処理水を
陰極室内に導入する循環路と、陰極室内の処理水を排出
する排出路と、陽極と陰極間に直流電圧を印加する電源
とを備えた装置にある。
[Means for Solving the Problems] In order to achieve the above object, the present invention provides a method in which treated water is placed in an electrolytic cell in which an anode chamber and a cathode chamber are formed by partitioning an anode and a cathode with a diaphragm. And then neutralized by flowing to the cathode chamber, and the anode is placed on the periphery and the cathode is arranged in the center, and the electrolyte is separated by a diaphragm. A tank, treated water supply means for supplying treated water into the anode chamber of the electrolytic cell, a circulation path for introducing treated water in the anode chamber into the cathode chamber, a discharge path for discharging treated water in the cathode chamber, and an anode. And a power supply for applying a DC voltage between the cathodes.

すなわち、本願請求項1に係る発明は、無菌水の製造
方法において、陽極と陰極間を隔膜で仕切って陽極室と
陰極室とを形成した電解槽内に、処理水を、陽極室に流
して酸性化して無菌水化したのち、陰極室へ流して中和
することを特徴とする。そして、本願請求項2に係る発
明は、無菌水の製造装置において、周面に陽極の筒を有
し中央に陰極が配置されると共にその間を隔膜で仕切ら
れた電解槽と、その電解槽の陽極室内に処理水を供給す
る処理水供給手段と、陽極室内の酸性化された処理水を
陰極室内に導入する循環路と、陰極室内の処理水を排出
する排水路と、陽極と陰極間に直流電圧を印加する電源
とを備えたことを特徴とする。
That is, the invention according to claim 1 of the present application is directed to a method for producing aseptic water, wherein treated water is flowed into an anode chamber in an electrolytic cell in which an anode and a cathode are partitioned by a diaphragm to form an anode chamber and a cathode chamber. It is characterized in that it is acidified to make it sterile water, and then it is made to flow into a cathode chamber for neutralization. The invention according to claim 2 of the present application is directed to an apparatus for producing sterile water, wherein an electrolytic cell having an anode cylinder on the peripheral surface and a cathode disposed in the center and having a diaphragm interposed therebetween, A treated water supply means for supplying treated water into the anode chamber, a circulation path for introducing acidified treated water in the anode chamber into the cathode chamber, a drainage path for discharging treated water in the cathode chamber, and between the anode and the cathode. And a power supply for applying a DC voltage.

[作用] 上記構成によれば、電解槽の陽極室から流出する酸性
水を陰極室へ導入し、電場内において中性水を生成し、
電場内において菌の生態系を破壊し、殺菌及び静菌を可
能にならしめ、安定した電解水の生成を流水状態で大量
の中性水の無菌水を生成できる。
[Action] According to the above configuration, the acidic water flowing out of the anode chamber of the electrolytic cell is introduced into the cathode chamber, and neutral water is generated in the electric field.
In the electric field, the ecosystem of bacteria is destroyed, sterilization and bacteriostasis are made possible, and stable generation of electrolyzed water can be performed in a flowing state to produce a large amount of sterile water with neutral water.

処理水としては通常の菌を含有する一般水を用い原水
の電気電導度が高い場合には、添加装置を稼動させるこ
となく、流水状態で大量の無菌水を、また電気電導度の
低い場合には、無機質の特に好ましくはNaCl等の添加液
で原水の電気電導度を高め、流水状態で大量の無菌水を
生成する。
When the electrical conductivity of raw water is high using ordinary water containing ordinary bacteria as the treated water, a large amount of sterile water in flowing water without operating the addition device, and when the electrical conductivity is low, Increases the electric conductivity of raw water with an inorganic liquid, particularly preferably NaCl or the like, and generates a large amount of sterile water in flowing water.

[実施例] 以下本発明の好適実施例を添付図面に基づいて説明す
る。
EXAMPLES Preferred embodiments of the present invention will be described below with reference to the accompanying drawings.

添付図において、1は電解槽であり、それぞれ非導電
材よりなる底板部2と蓋板部4と、その間で円筒状の外
周を構成するステンレス製等の陽極3からなる。蓋板部
4には電解槽1の内部に延びる陰極5及びこれを電源23
に接続するための陰極ターミナル6が配置され、また、
前記陽極3には、電源23に接続される陽極ターミナル7
が配置される。さらに電解槽1は陰極5を囲むように円
筒状の隔膜8が設けられ、この隔膜8により電解槽1内
が陰極室9と陽極室10に区画される。また底板部2には
電解槽1の陽極室10に処理水を供給するための導入口14
が設けられ、また蓋板部4には陽極室10の処理水の出口
16が設けられ、その出口16が循環路15を介して蓋板部4
に設けた陰極側導入口17に接続される。さらに蓋板部4
には陰極室9内の処理水の出口19が設けられ、その出口
19に排出路18が接続される。
In the accompanying drawings, reference numeral 1 denotes an electrolytic cell, which comprises a bottom plate portion 2 and a cover plate portion 4 each made of a non-conductive material, and an anode 3 made of stainless steel or the like forming a cylindrical outer periphery therebetween. The cover plate 4 includes a cathode 5 extending into the electrolytic cell 1 and a power source 23.
A cathode terminal 6 for connecting to
The anode 3 has an anode terminal 7 connected to a power source 23.
Is arranged. Further, the electrolytic cell 1 is provided with a cylindrical diaphragm 8 surrounding the cathode 5, and the inside of the electrolytic cell 1 is partitioned into a cathode chamber 9 and an anode chamber 10 by the diaphragm 8. The bottom plate 2 has an inlet 14 for supplying treated water to the anode chamber 10 of the electrolytic cell 1.
The cover plate 4 has an outlet for treated water in the anode chamber 10.
16 is provided, and the outlet 16 is connected to the cover plate 4
Is connected to the cathode-side inlet 17 provided at the second position. Further, the cover plate 4
Is provided with an outlet 19 for treated water in the cathode chamber 9, and the outlet
The discharge path 18 is connected to 19.

陽極室10へ導入する処理水の導入口14には、処理水供
給手段24が接続される。この処理水供給手段24は、原水
導入パイプ11、バルブ12、継手20、パイプ13を通して、
陽極室10へ水道水などの原水を供給するライン24aと、N
aCl溶液など無機質液22をポンプ注入装置21より接続継
手20を介して原水中に添加液を混入して処理水の電気電
導度を調節する添加液ライン24bとからなる。
A treated water supply means 24 is connected to the treated water introduction port 14 introduced into the anode chamber 10. This treated water supply means 24 passes through the raw water introduction pipe 11, the valve 12, the fitting 20, and the pipe 13,
A line 24a for supplying raw water such as tap water to the anode chamber 10;
An additive liquid line 24b for adjusting the electric conductivity of the treated water by mixing an additive liquid such as an aCl solution from the pump injection device 21 into the raw water via the connection joint 20 through the connection joint 20.

この処理水供給手段24において、井水、水道水は一般
的に電気電導度の不安定かつ各他方によって異なってい
るために、原水の電気電導度を上げ、電解効率をよくす
るためにポンプ注入装置21により無機質液23を添加す
る。また、原水供給に際して、加圧用ポンプ等は図示し
てないが、電解槽1での電解効率、電解速度等に比例し
て、加圧状態で原水を供給しても良く、その場合には、
ポンプを使用すれば良い。
In this treated water supply means 24, well water and tap water generally have unstable electric conductivities and differ from each other. Therefore, pumping is performed to increase electric conductivity of raw water and improve electrolytic efficiency. The inorganic liquid 23 is added by the device 21. In supplying the raw water, a pressurizing pump and the like are not shown, but the raw water may be supplied in a pressurized state in proportion to the electrolysis efficiency in the electrolytic cell 1, the electrolysis speed, and the like.
You can use a pump.

排出路18からの処理水は、食品加工用の水槽、プー
ル、貯水槽に供給してもよく、また本実施例に対しては
食品加工用の水槽、プール、貯水槽の水を原水として、
前記ポンプなどにより加圧状態にし、原水導入パイプ11
から電解槽1へと導き、電解槽1で処理された水を排出
路18を通り、前記の原水へと循環させてもよく、また菌
におかされた原水を、例えば水道水、井水、排水処理
水、屎尿処理水として、ポンプ等により加圧状態で、原
水導入パイプ11から電解槽1を経て排出路18を通り下水
へと放流してもよいものである。
The treated water from the discharge channel 18 may be supplied to a water tank for food processing, a pool, a water storage tank, and for this embodiment, water in the water tank for food processing, a pool, a water storage tank is used as raw water,
Pressurized by the pump and the like, and the raw water introduction pipe 11
To the electrolytic cell 1, the water treated in the electrolytic cell 1 may be circulated through the discharge path 18 to the raw water, and the raw water disinfected by bacteria may be, for example, tap water, well water, The treated wastewater and the treated human wastewater may be discharged from the raw water introduction pipe 11 through the electrolytic tank 1 through the discharge passage 18 to the sewage in a pressurized state by a pump or the like.

次に本発明の無菌水を製造する方法について説明す
る。
Next, a method for producing sterile water of the present invention will be described.

最初に原水の電気電導度が所望で有るか否かの判断確
認後、電気電導度の低い場合は、無機質液22をポンプ注
入装置21で注入し所望の原水の電気電導度にして送水す
る。また、原水及び電気電導度を高めた原水が電解槽1
の陽極側導入口14を通り陽極室10に供給される。
First, after confirming whether or not the electric conductivity of the raw water is desired, if the electric conductivity is low, the inorganic liquid 22 is injected by the pump injection device 21 to supply the desired electric conductivity of the raw water and water is supplied. In addition, the raw water and the raw water with the increased electric conductivity are supplied to the electrolytic cell 1.
Is supplied to the anode chamber 10 through the anode-side inlet 14.

陽極室10から排出された水は循環路15を通り、陰極室
9に導かれる陰極側導入口17を通り陰極室9に導かれ、
陰極側排出口19から排出される。そして前記電解槽1の
陽極側排出口16から酸性水が、循環路15を通り、陰極室
9に充満してから後、所定電圧の直流電源を陽極電極3
及び陰極電極5に加えるために、電源23より電極ターミ
ナル6,7に印加する。そうすれば、所定の流量及び所定
の印加電圧を加えれば陽極室10側においては所定のpHの
酸性水が生成される。また、循環路15を通り供給された
酸性水は陰極側へ導かれ、陰極室9側においては、電気
化学反応によりアルカリ水が発生し、酸性水と混合中和
され中性水として陰極側排出口19より排出され、中性の
無菌水とするものである。
The water discharged from the anode chamber 10 passes through the circulation path 15 and is guided to the cathode chamber 9 through the cathode-side inlet 17 guided to the cathode chamber 9,
It is discharged from the cathode outlet 19. After the acidic water is filled from the anode side discharge port 16 of the electrolytic cell 1 through the circulation path 15 into the cathode chamber 9, a DC power supply of a predetermined voltage is applied to the anode electrode 3.
In addition, the power is applied to the electrode terminals 6 and 7 from the power supply 23 in order to apply the voltage to the cathode electrode 5. Then, when a predetermined flow rate and a predetermined applied voltage are applied, acidic water having a predetermined pH is generated on the anode chamber 10 side. Further, the acidic water supplied through the circulation path 15 is guided to the cathode side, and in the cathode chamber 9 side, alkaline water is generated by an electrochemical reaction, mixed and neutralized with the acidic water, and discharged as neutral water on the cathode side. It is discharged from the outlet 19 and becomes neutral sterile water.

以上の方法により殺菌した場合の結果の実験例を第1
表に示す。
The experimental example of the result when sterilized by the above method is
It is shown in the table.

この実験に際し、使用した被処理水試料としては、水
道水に腐敗した豆腐、生ウドンをホモナイズしたもの
と、純粋培養した大腸菌群を混入されたものを原水とし
て流量1000ml/分のもとで電解したもので、実験例と
して、一般細菌と大腸菌群数を上記第1表に表わしたも
のである。
In this experiment, the to-be-treated water sample used was a homogenized tofu and raw uddon that had been spoiled in tap water, and a sample mixed with purely cultured Escherichia coli as raw water and electrolyzed at a flow rate of 1000 ml / min. As an experimental example, the numbers of common bacteria and coliform bacteria are shown in Table 1 above.

さらに、本発明の無菌水の製造方法または製造装置の
効果を比較するために実験例を、本実施例の電極特性
をプラス。マイナ反転させ殺菌させた場合の結果を第2
表に示す。条件としの被処理水試料は第1表の条件と同
じにしてあり、一般細菌と大腸菌群数を表わしている。
Further, an experimental example was used to compare the effects of the method or apparatus for producing sterile water of the present invention, and the electrode characteristics of the present example were added. The result of minor reversal and sterilization is
It is shown in the table. The treated water sample as the condition is the same as the condition in Table 1, and represents the number of general bacteria and coliforms.

上記実施例におけるデータを、実験例,に基づい
て詳細に検討すると、実験例では、大腸菌群及び一般
細菌群の存在する原水を電解処理される陽極室の酸性水
でのpH3.70以下では殺菌効果があり、さらにより殺菌効
果を上げるためには、pH3.49以下であれば完全に死滅し
ていることを知り得る。
Examination of the data in the above example in detail based on an experimental example shows that in the experimental example, the raw water containing the coliform bacteria and general bacteria was sterilized at pH 3.70 or lower in the acidic water in the anode chamber subjected to electrolytic treatment. It is effective, and in order to further improve the bactericidal effect, it can be known that the cells are completely killed if the pH is 3.49 or less.

さらに、本実施例による実験例と比較するために実験
例として大腸菌群がpHによる殺菌効果を知るために、
電気分解をした酸性水のpHとその殺菌の挙動を調べた結
果を第3表に示す。
Furthermore, in order to compare the experimental example according to the present embodiment, as an experimental example, the coliform group to know the bactericidal effect by pH,
Table 3 shows the results of examining the pH of the electrolyzed acidic water and the sterilizing behavior thereof.

第3表において電解された酸性水ではpH2.70以下でな
ければ大腸菌群は完全に死滅することがなかったのに対
して、本実施例の実験例の第1表ではpH3.49以下であ
れば完全に効果を示している。この見地から解ること
は、電場内において酸性水は、殺菌に対して、電気化学
エネルギーによる酸化反応が高いものと判断でき、pHが
高くても高い殺菌効果が生じるものと思慮される。
In Table 3, in the case of the electrolyzed acidic water, the coliforms were not completely killed unless the pH was 2.70 or less, whereas in Table 1 of the experimental example of this example, the pH was 3.49 or less. It is completely effective. From this point of view, it can be considered that acidic water in an electric field has a high oxidation reaction by electrochemical energy with respect to sterilization, and it is considered that a high sterilizing effect is produced even if the pH is high.

さらに、実験例と殺菌効果を比較するために、実験
例の電極特性をプラスとマイナスとを反転させ印加し
た場合の殺菌効果の実験例を第2表より比較すると、殺
菌効果は全く現われていないことを意味している。
Furthermore, in order to compare the sterilizing effect with the experimental example, when comparing the experimental example of the sterilizing effect when the electrode characteristics of the experimental example were inverted and applied from Table 2, the sterilizing effect did not appear at all. Means that.

このとは電解電場内でアルカリ水が陽極側で単に中性
化反応しているために、菌に対して完全に酸化反応が起
らなかったことを意味している。また原水の電気電導度
の変化に対する電解効率を第4表に示す。
This means that the oxidation reaction did not completely occur for the bacteria because the alkaline water was simply neutralized on the anode side in the electrolytic electric field. Table 4 shows the electrolysis efficiency with respect to the change in the electric conductivity of the raw water.

この表から解ることは、所定のpHを得るためには、電
気電導度が低いと、消費電力が大きく、また電気電導度
が高いと、消費電力が小さくてすむことを表わし、多量
の中性無菌水を得る場合には、例えばNaCl等の無機物質
を添加して原水の電気電導度を上げ、電解効率を上げる
ことが効果的であることが解る。
From this table, it can be seen that, in order to obtain a predetermined pH, low electric conductivity requires high power consumption, and high electric conductivity requires low power consumption. In the case of obtaining sterile water, it is found that it is effective to increase the electric conductivity of raw water by adding an inorganic substance such as NaCl to increase the electrolysis efficiency.

すなわち、本実施例の実験例からすれば酸性水を陰
極室へ導入し、電解されると、中性化され、その殺菌効
果は無菌状態を維持した無菌水が生成されることにな
る。
That is, according to the experimental example of the present embodiment, when acidic water is introduced into the cathode chamber and electrolyzed, it is neutralized, and the sterilizing effect of the sterilized water is maintained.

[発明の効果] 本発明によれば、一般水を電気分解すること、また原
水の電気電導度による不安定な無菌水を生成することを
なくすために、無機質添加装置により原水に混合して、
電気分解すること、及びこれによって得られる電解水を
利用し、常温下において、流水状態のまま、しかも簡易
な機構に係る設備のみで、一般流水を無菌にすると共に
循環水等の細菌に汚染された水を殺菌することができ
る。
[Effects of the Invention] According to the present invention, in order to eliminate the generation of unstable sterile water due to the electroconductivity of raw water and the electrical conductivity of raw water, the raw water is mixed with raw water by an inorganic addition device,
Electrolyzing, and using the electrolyzed water obtained by this, at room temperature, in a running water state, and with only the equipment related to a simple mechanism, sterilization of general running water and contamination by bacteria such as circulating water Water can be sterilized.

このことは、従来の化学薬剤以外には常温下、流水状
態下で、その細菌汚染された水を無菌状態に生成すると
いう技術がなかっただけに、多種多様の無菌水を利用し
て消毒殺菌、洗浄等を必要とする分野で、例えば食品加
工用の水、水泳用プール水、建物内外に設置される土木
用の貯水槽内の水及び空調用クーラ及びクーラボックス
に使用するクーラ水等の無菌または静菌状態での水処理
が好ましい場合の、その無菌水を簡易に提供できるもの
である。
This is because, apart from conventional chemical agents, there was no technology to produce the bacteria-contaminated water under sterile conditions at normal temperature and in flowing water. In fields that require cleaning, such as water for food processing, pool water for swimming, water in water storage tanks for civil engineering installed inside and outside the building, and cooler water used for air conditioning coolers and cooler boxes, etc. When sterile or bacteriostatic water treatment is preferred, the sterile water can be easily provided.

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

添付図面は本発明の一実施例を示す断面図である。 図中、1は電解槽、3は陽極、5は陰極、9は陰極室、
10は陽極室である。
The accompanying drawings are sectional views showing one embodiment of the present invention. In the figure, 1 is an electrolytic cell, 3 is an anode, 5 is a cathode, 9 is a cathode chamber,
10 is an anode chamber.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】陽極と陰極間を隔膜で仕切って陽極室と陰
極室とを形成した電解槽内に、処理水を、陽極室に流し
て酸性化して無菌水化したのち、陰極室へ流して中和す
ることを特徴とする無菌水の製造方法。
In an electrolytic cell having an anode compartment and a cathode compartment formed by partitioning an anode and a cathode by a diaphragm, treated water is made to flow into the anode compartment to be acidified and sterilized, and then to the cathode compartment. A method for producing sterile water, wherein the sterilization water is neutralized.
【請求項2】周面に陽極の筒を有し中央に陰極が配置さ
れると共にその間を隔膜で仕切られた電解槽と、その電
解槽の陽極室内に処理水を供給する処理水供給手段と、
陽極室内の酸性化された処理水を陰極室内に導入する循
環路と、陰極室内の処理水を排出する排水路と、陽極と
陰極間に直流電圧を印加する電源とを備えたことを特徴
とする無菌水の製造装置。
2. An electrolytic cell having an anode cylinder on the peripheral surface, a cathode disposed in the center, and a diaphragm interposed therebetween, and treated water supply means for supplying treated water into the anode chamber of the electrolytic cell. ,
A circulation path for introducing the acidified treated water in the anode chamber into the cathode chamber, a drainage path for discharging the treated water in the cathode chamber, and a power supply for applying a DC voltage between the anode and the cathode. Sterile water production equipment.
JP63051765A 1988-03-07 1988-03-07 Method and apparatus for producing sterile water Expired - Lifetime JP2714662B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63051765A JP2714662B2 (en) 1988-03-07 1988-03-07 Method and apparatus for producing sterile water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63051765A JP2714662B2 (en) 1988-03-07 1988-03-07 Method and apparatus for producing sterile water

Publications (2)

Publication Number Publication Date
JPH01228589A JPH01228589A (en) 1989-09-12
JP2714662B2 true JP2714662B2 (en) 1998-02-16

Family

ID=12896045

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63051765A Expired - Lifetime JP2714662B2 (en) 1988-03-07 1988-03-07 Method and apparatus for producing sterile water

Country Status (1)

Country Link
JP (1) JP2714662B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04330986A (en) * 1991-04-30 1992-11-18 Yukiaki Matsuo Production of free chlorine water and equipment therefor
AU2829300A (en) 1999-03-24 2000-10-09 Ebara Corporation Method and apparatus for detecting negative ion in water
EP1285884A4 (en) * 2000-04-27 2005-06-01 Nippon Oil Corp Method and apparatus for clarification treatment of water
JP2005254101A (en) * 2004-03-10 2005-09-22 Hoshizaki Electric Co Ltd Electrolytic method and device

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5879587A (en) * 1981-11-05 1983-05-13 Tatsuro Nakayama Producing device for alkali ion water
JPS59189988A (en) * 1983-04-12 1984-10-27 Tatsuo Okazaki Controlling mechanism for volume of water in continuous water electrolysis unit

Also Published As

Publication number Publication date
JPH01228589A (en) 1989-09-12

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