JPH0499295A - Electrolyzed water straightening equipment - Google Patents

Electrolyzed water straightening equipment

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Publication number
JPH0499295A
JPH0499295A JP2213282A JP21328290A JPH0499295A JP H0499295 A JPH0499295 A JP H0499295A JP 2213282 A JP2213282 A JP 2213282A JP 21328290 A JP21328290 A JP 21328290A JP H0499295 A JPH0499295 A JP H0499295A
Authority
JP
Japan
Prior art keywords
water
pair
neutralizer
electrolytic
neutralizing agent
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
JP2213282A
Other languages
Japanese (ja)
Inventor
Tatsuo Okazaki
龍夫 岡崎
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 JP2213282A priority Critical patent/JPH0499295A/en
Publication of JPH0499295A publication Critical patent/JPH0499295A/en
Pending legal-status Critical Current

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  • Water Treatment By Electricity Or Magnetism (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

PURPOSE:To offer an electrolyzed water straightening equipment with which alkali water or acid water can be obtained by the same amt. as that of supplied source water without largely changing pH of the water in the electrolysis cell to be used by selectively opening and closing a neutralizer supplying circuit comprising two systems, one being to supply a neutralizer for acid to the cathode room in the electrolytic cell and the other being to supply a neutralizer for alkali to the anode room. CONSTITUTION:A neutralizer supplying circuit 9 from a tank 13 of neutralizer for alkali water is opened with a valve device 11. Then the neutralizer for alkali water is introduced to the cathode room 2 by a pump 14. On the other hand, a neutralizer supplying circuit 10 from a tank 12 of a neutralizer for acidic water is closed with a valve device 11. Acidic water from the anode room 3' and neutralized water (e.g. neutral water) from the cathode room 2' are joined in a common tube 8 and drained through a water drainer 15 such as a shower head or tap. Since the electrolyzed water in the cathode room 2' is almost neutralized, the joined water is maintained acidic. Thereby, acidic water is discharged from the water drainer 15 by the amt. equivalent to the total amt. of the supplied water.

Description

【発明の詳細な説明】 〔発明の利用分野〕 関し、特に、電解中に一方の電極室の水を中和し、他方
の電極室の電解水に合流して排出する電解整水装置に関
する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] In particular, the present invention relates to an electrolytic water conditioning device that neutralizes water in one electrode chamber during electrolysis, merges with electrolyzed water in the other electrode chamber, and discharges the water.

j発明が解決しようとする課8″′。j Problem 8''' that the invention seeks to solve.

水を電角ゼして飲用のアルカリイオン水または酸性イオ
ン水を生成する従来の電解水生成装置は、アルカリ水と
酸性水の各排水管路が独立しており、アルカリ水を使用
する場合は酸性水をドレンへ捨て、酸性水を使用する場
合はアルカリ水をドレンへ捨てる構造になっている。こ
のため、給水路から供給する原水量に対し、利用側電解
水の歩留まりか悪い。
Conventional electrolyzed water generation equipment that generates drinking alkaline ionized water or acidic ionized water by electrolyzing water has separate drainage pipes for alkaline water and acidic water, and when using alkaline water, The structure is such that acidic water is disposed of into the drain, and when acidic water is used, alkaline water is disposed of into the drain. For this reason, the yield of electrolyzed water on the user side is poor compared to the amount of raw water supplied from the water supply channel.

本発明の目的は使用側電解水のPH値を大きく変化させ
ずに供給原水と同量のアルカリ水または酸性水を選択的
に得る電解整水装置を提供することにある。
An object of the present invention is to provide an electrolytic water conditioning device that selectively obtains the same amount of alkaline water or acidic water as the raw water to be supplied without significantly changing the pH value of the electrolyzed water on the user side.

[課題を解決するための手段〕 一4二記目的を達成するために、本発明の電解整水装置
は、極性の異なる一対の電極間を電解隔膜によって一対
の電極室に区画した電解槽を具備し、この電解槽の一側
に給水管路を設けるとともに、他側に前記各々の電極室
に連通ずる一対の電解水排水管路を合流させて排出する
電解水取水管路を設けた水の電解装置と、電解槽の陰極
室に酸性中和剤を供給し、陽極室にアルカリ中和剤を供
給する二系統の中和剤供給回路と、二系統の中和剤供給
回路の途中に設けられ、これら二系統の中和剤供給回路
を選択的に開閉する選択バルブ装置とを具備している。
[Means for Solving the Problems] In order to achieve the object No. 142, the electrolytic water conditioning device of the present invention includes an electrolytic cell in which a pair of electrodes with different polarities is partitioned into a pair of electrode chambers by an electrolytic diaphragm. A water supply pipe is provided on one side of the electrolytic cell, and an electrolyzed water intake pipe is provided on the other side for merging and discharging a pair of electrolyzed water drainage pipes communicating with each of the electrode chambers. electrolyzer, a two-system neutralizer supply circuit that supplies an acidic neutralizer to the cathode chamber of the electrolytic cell, and an alkaline neutralizer to the anode chamber, and a neutralizer supply circuit that supplies two systems in the middle of the two-system neutralizer supply circuit. and a selection valve device that selectively opens and closes these two neutralizing agent supply circuits.

また、さらに好ましくは、上記電解装置の一対の電極を
印加電圧の極性を切り換えて連続的に電解できる陰極・
陽極両用の電極で構成するとともに、電解装置の電源回
路に電圧極性切換制御部を具備し、さらに、前記二系統
の中和剤供給管路に前記電圧極性切換制御部の作動に連
動してこれら二系統の中和剤供給管路の流路を切換える
切換バルブを設けてもよい。
More preferably, the pair of electrodes of the electrolysis device is a cathode capable of continuously electrolyzing by switching the polarity of the applied voltage.
In addition to being composed of an electrode that can be used as an anode, the power supply circuit of the electrolyzer is equipped with a voltage polarity switching control section, and furthermore, the two systems of neutralizing agent supply conduits are connected to these two systems in conjunction with the operation of the voltage polarity switching control section. A switching valve may be provided to switch the flow paths of the two systems of neutralizing agent supply pipes.

いずれの場合も電解装置の一対の電解水取水管路に流量
比調整バルブを設けるのが望ましい。特に、陰極・陽極
両用の電極を使用し、印加電圧の極性を切換えて連続的
に電解する装置の場合は電解装置の一対の電解水排水管
路に、電圧極性切換制御部の切換えに連動して該一対の
電解水排水流量を所定流量比に調整する流量比調整バル
ブを設ける。
In either case, it is desirable to provide a flow ratio adjustment valve in a pair of electrolyzed water intake pipes of the electrolyzer. In particular, in the case of a device that uses both cathode and anode electrodes and performs continuous electrolysis by switching the polarity of the applied voltage, a pair of electrolyzed water drainage pipes in the electrolysis device is linked to the switching of the voltage polarity switching control section. A flow rate ratio adjustment valve is provided to adjust the pair of electrolyzed water drainage flow rates to a predetermined flow rate ratio.

:発明の作用〕 本発明の装置は中和剤を添加した電極室の水が電解中に
中和され、他方の電解質の水は目的のアルカリ水または
酸性水に電解される。これら画電極室の電解水は合流さ
れて共通の取水口から排出されるが、一方の電解水は中
和されているので目的の他方の電極室の電解水にこれを
混合しても全体のpHには大きな変動がない。従って、
供給原水の全量が目的の電解水(アルカリ水または酸性
水)として利用に供される。
: Effect of the invention] In the apparatus of the present invention, the water in the electrode chamber to which a neutralizing agent has been added is neutralized during electrolysis, and the water in the other electrolyte is electrolyzed to the target alkaline water or acidic water. The electrolyzed water in these picture electrode chambers is combined and discharged from a common water intake, but since the electrolyzed water in one is neutralized, even if it is mixed with the electrolyzed water in the other electrode chamber, the total There are no large fluctuations in pH. Therefore,
The entire amount of supplied raw water is used as the target electrolyzed water (alkaline water or acidic water).

酸性水中和剤とアルカリ水中1[]剤の二系統の中和剤
供給回路をバルブ装置によって選択的に開閉することに
より、酸性水及びアルカリ水の中和が任意に切り換えら
れる。
Neutralization of acidic water and alkaline water can be arbitrarily switched by selectively opening and closing two systems of neutralizing agent supply circuits, one for acidic water dispersible and one for alkaline water, using a valve device.

電解装置の一対の電極を印加電圧の極性を切り換えて連
続的に電解できる陰極・陽極両用の電極で構成するとと
もに、電解装置の電源回路に電圧極性切換制御部を具備
し、さらに、前記二系統の中和剤供給管路に前記電圧極
性切換制御部の作動に連動してこれら二系統の中和剤供
給管路の流路を切換える切換バルブを設けた場合は印加
電圧の切換えによって電極室に生成される水の性質が逆
になるが、これと同時に中和剤の流路も切換わるので取
水蛇口からは引続き所望の性質の電解水が得られる。
The pair of electrodes of the electrolysis device is composed of a cathode/anode electrode that can perform continuous electrolysis by switching the polarity of the applied voltage, and the power supply circuit of the electrolysis device is equipped with a voltage polarity switching control section, and furthermore, the two systems are If the neutralizing agent supply line is provided with a switching valve that switches the flow paths of these two systems of neutralizing agent supply lines in conjunction with the operation of the voltage polarity switching control section, the voltage applied to the electrode chamber can be changed by switching the applied voltage. The properties of the produced water are reversed, but at the same time, the flow path of the neutralizer is also switched, so electrolyzed water with the desired properties can still be obtained from the water intake faucet.

この種の電解装置は目的に応じてアルカリ水と酸性水の
生成比率(流量)を異ならせる場合かあるがその調整は
一対の電解水排水管路に設けた流量比調整バルブによっ
て調節される。特に、電解電圧の極性を切換えて運転さ
れる電解装置にあってはこの流量比調整バルブは電極の
極性切換えに連動し、所定の流量比を保持するように作
動する。
In this type of electrolyzer, the production ratio (flow rate) of alkaline water and acidic water may be varied depending on the purpose, but this adjustment is controlled by a flow rate ratio adjustment valve provided in a pair of electrolyzed water drainage pipes. In particular, in an electrolytic device that is operated by switching the polarity of the electrolytic voltage, this flow rate ratio adjustment valve operates in conjunction with the switching of the electrode polarity to maintain a predetermined flow rate ratio.

〔発明の実施例〕[Embodiments of the invention]

以下、本発明の実施例を添付図面に基づいて説明する。 Embodiments of the present invention will be described below with reference to the accompanying drawings.

図において1は対向配置した異極性の電極2゜3間を電
解隔膜4によって一対の電極室2′3′に仕切った電解
槽1′を具備する電解装置である。
In the figure, reference numeral 1 denotes an electrolytic device equipped with an electrolytic cell 1' in which a pair of electrode chambers 2' and 3' are partitioned by an electrolytic diaphragm 4 between electrodes 2 and 3 of opposite polarity arranged oppositely.

電解槽1′の一側には水道水等の原水を供給する給水管
路5が設けられており、他側には各々の電極室2’、3
’ に個別に連通ずる一対の排水管6.7が接続されて
いる。
A water supply pipe 5 for supplying raw water such as tap water is provided on one side of the electrolytic cell 1', and electrode chambers 2' and 3 are provided on the other side.
A pair of drain pipes 6.7 are connected to the drain pipes 6 and 7, which communicate with each other individually.

かくして電源回路Eから電極2,3に直流の電解電圧を
印加することにより、電解槽1に導入された原水が電解
される。
By thus applying a direct current electrolytic voltage from the power supply circuit E to the electrodes 2 and 3, the raw water introduced into the electrolytic cell 1 is electrolyzed.

本発明に用いられる上記電解装置は、陰極室2′及び陽
極室3′に連通ずる前記一対の排水管路67を合流させ
、共通の取水管路8から取出すようになっている。
In the electrolyzer used in the present invention, the pair of drain pipes 67 communicating with the cathode chamber 2' and the anode chamber 3' are merged, and water is taken out from a common water intake pipe 8.

電解槽1′の陰極室2′にはここに生成されるアルカリ
水を必要に応じて中和するためのアルカリ水用中和剤供
給回路9が配管されているとともに、陽極室3′にはこ
こに生成される酸性水を必要に応して中和するための酸
性水用中和剤供給回路10が配管されている。
The cathode chamber 2' of the electrolytic cell 1' is equipped with an alkaline water neutralizer supply circuit 9 for neutralizing the alkaline water produced there as required, and the anode chamber 3' is equipped with an alkaline water neutralizer supply circuit 9. A neutralizing agent supply circuit 10 for acidic water is piped therein to neutralize the acidic water generated here as necessary.

二系統の中和剤供給回路9.10はこれら中和剤供給回
路9.10を択一的に選択開閉するバルブ装置11を介
して各々の対応する中和剤タンク12.13に接続され
ている。
The two systems of neutralizing agent supply circuits 9.10 are connected to each corresponding neutralizing agent tank 12.13 via a valve device 11 that selectively opens and closes these neutralizing agent supply circuits 9.10. There is.

バルブ装置11は図に例示した構造に限らず、二系統の
通路9,10の一方が開いているときに他方か閉じるよ
うに択一的に開閉するものであれば他のいかなる構造の
ものでもよい。
The valve device 11 is not limited to the structure illustrated in the figure, but may have any other structure as long as it can be selectively opened and closed so that when one of the two passages 9 and 10 is open, the other is closed. good.

か(して、第1図の状態ではバルブ装置11によってア
ルカリ水用中和剤タンク13からの中和剤供給回路9が
開いているのでポンプ14によってアルカリ水用の中和
剤が陰極室2′に添加され、他方、酸性水用中和剤タン
ク12からの中和剤供給回路10はバルブ装置11によ
って閉鎖されている。この状態では、電解によって陽極
室3′に酸性水が生成され、排水管路6から排出されに
対し、陰極室2′の水はタンク13からの中和剤によっ
て例えばほぼPH7、あるいはそれ以下に中和された水
となって排水管路7から排出される。
In the state shown in FIG. ', and on the other hand, the neutralizer supply circuit 10 from the acidic water neutralizer tank 12 is closed by the valve device 11. In this state, acidic water is produced in the anode chamber 3' by electrolysis, The water in the cathode chamber 2' is discharged from the drain pipe 7, while the water in the cathode chamber 2' is neutralized to approximately pH 7 or lower by the neutralizing agent from the tank 13, and is discharged from the drain pipe 7.

かくして陽極室3′からの酸性水と陰極室2′からの中
和水(例えば中性の水)が共通の取水管路8に合流され
、シャワー、蛇口などの取水部15から排出されるが、
陰極室2′の電解水はほぼ中性に中和されているので合
流後の水は酸性に維持される。従って取水部15からは
供給原水の全j11に見合う酸性水か排出される。
In this way, the acidic water from the anode chamber 3' and the neutralized water (for example, neutral water) from the cathode chamber 2' are combined into the common water intake pipe 8 and discharged from the water intake part 15 such as a shower or faucet. ,
Since the electrolyzed water in the cathode chamber 2' has been neutralized to approximately neutrality, the water after merging is maintained at an acidic level. Therefore, from the water intake section 15, acidic water corresponding to the total amount of raw water j11 is discharged.

他方、バルブ装置11を操作して酸性水の中和剤供給回
路10が開き、アルカリ水中和剤供給回路9か閉しるよ
うに流路を切り換えると、陰極室2′からアルカリ水が
排出され、陽極室3′の水は中和剤によりほぼPH7ま
たはそれ以上に中和される。従って、上記と逆に取水部
15からは供給原水の全量がアルカリ水として排出され
る。
On the other hand, when the valve device 11 is operated to switch the flow path so that the neutralizing agent supply circuit 10 for acidic water is opened and the neutralizing agent supply circuit 9 for alkaline water is closed, alkaline water is discharged from the cathode chamber 2'. The water in the anode chamber 3' is neutralized to approximately pH 7 or higher by the neutralizing agent. Therefore, contrary to the above, the entire amount of supplied raw water is discharged from the water intake section 15 as alkaline water.

バルブ装置11は蛇ロレバー簿で機械的に切換操作する
構造でもよく、また取付部15五傍のスイッチにより電
気的に切換操作する構造にしてもよい。
The valve device 11 may have a structure in which the switching operation is performed mechanically using a serpentine lever, or may have a structure in which the switching operation is performed electrically by a switch near the mounting portion 15.

尚、画電極室の流量比率は生成しようとする水の性質に
よって必ずしも一定ではない。このため、一対の排水管
路6,7(好ましくはその合流部)に流量比調整バルブ
16を設け、流量比率を調節できるようにしておくのが
望ましい。
Note that the flow rate ratio of the picture electrode chamber is not necessarily constant depending on the nature of the water to be produced. For this reason, it is desirable to provide a flow rate ratio adjustment valve 16 in the pair of drain pipes 6 and 7 (preferably at their confluence) so that the flow rate ratio can be adjusted.

第2図は本発明の他の実施例を示すもので この実施例
では電解槽1′の一対の電極2,3を印加電圧の極性を
切り換えて連続的に電解できる陰極・陽極両用の電極で
構成するとともに、電解装置1の電源回路Eに電圧極性
切換制御部17を設け、さらに、二系統の中和剤供給管
路9,1oに前記電圧極性切換制御部の作動に連動して
これら二系統の中和剤供給管路9,10の流路を切換え
る切換バルブ18を介したものである。
Fig. 2 shows another embodiment of the present invention. In this embodiment, the pair of electrodes 2 and 3 of the electrolytic cell 1' are used as both cathode and anode electrodes that can perform continuous electrolysis by switching the polarity of the applied voltage. At the same time, a voltage polarity switching control section 17 is provided in the power supply circuit E of the electrolysis device 1, and furthermore, these two systems are connected to the two systems of neutralizing agent supply conduits 9 and 1o in conjunction with the operation of the voltage polarity switching control section. This is via a switching valve 18 that switches the flow paths of the neutralizer supply pipes 9 and 10 of the system.

水の電解装置lはアルカリイオン水の通る所にカルシウ
ムが析出し、種々の障害となり易い。
In a water electrolysis device 1, calcium is deposited where alkaline ionized water passes, which tends to cause various problems.

第2図のように、電極への印加電圧の極性を一定積算時
間毎に変換して電解することでこの問題は解決するが、
電極の極性変換により電極室が逆になるため、中和剤供
給回路9,1oの流路を切換える必要がある。切換バル
ブ18はそのために設けられているもので、第2図では
前記中和剤供給回路の選択バルブ装置]1の下流側に設
置しであるが、上流側に設けることももちろん可能であ
る。
As shown in Figure 2, this problem can be solved by changing the polarity of the voltage applied to the electrode at regular intervals for electrolysis.
Since the electrode chambers are reversed by changing the polarity of the electrodes, it is necessary to switch the flow paths of the neutralizing agent supply circuits 9 and 1o. The switching valve 18 is provided for this purpose, and although it is shown in FIG. 2 on the downstream side of the selection valve device 1 of the neutralizing agent supply circuit, it is of course possible to provide it on the upstream side.

第2図実施例は極性変換によって陰極室力陽極室に、ま
た、陽極室が陰極室に変わるが、これと連動して中和剤
の流路も切り換わるので、取水部15から得られる水は
極性変換の影響をうけない。
In the embodiment shown in FIG. 2, the polarity is changed to change the power of the cathode into the anode and the anode into the cathode. is not affected by polarity conversion.

それ以外の作用及び操作は第1図実施例と同じである。Other functions and operations are the same as in the embodiment shown in FIG.

尚、電圧の極性切換は手動でもよく、また電解時間を積
算して所定積算時間に達すると自動的に切り換わる方式
でもよい。
The polarity of the voltage may be switched manually or may be switched automatically when the electrolysis time is accumulated and a predetermined accumulated time is reached.

電解に際しては、中和剤供給回路を利用するかあるいは
別の供給路を設けて美容その他の薬剤を原水に添加する
ようにしてもよい。
During electrolysis, a neutralizing agent supply circuit may be used or a separate supply path may be provided to add cosmetic or other chemicals to the raw water.

図では連続通水式の電解装置を使用する場合を例示した
が、本発明はこれに限らずバッチ式電解〔発明の効果〕 本発明は電解水を生成する際に、従来槽てていた非利用
側の水を中和し、利用側の水に混合して排出するもので
あるが、中和された水を混合するので全体のPH値は大
きくは変らない。従って、供給原水の全量を使用目的の
水(アルカリ水または酸性水)として取水部から利用す
ることができ、無駄かない。
Although the figure shows an example in which a continuous water flow type electrolyzer is used, the present invention is not limited to this, and the present invention is applicable to batch type electrolysis when producing electrolyzed water. The water on the user side is neutralized and mixed with the water on the user side before being discharged, but since the neutralized water is mixed, the overall pH value does not change significantly. Therefore, the entire amount of supplied raw water can be used from the water intake section as water for the purpose of use (alkaline water or acidic water), so there is no waste.

また、中和剤供給回路の開閉を切換えることにより、ア
ルカリ水または酸性水の任意の電解水を共通の取水口か
ら選択的に取出すことかできる。
Moreover, by switching the opening and closing of the neutralizer supply circuit, any electrolyzed water, alkaline water or acidic water, can be selectively taken out from the common water intake port.

従って、多目的に利用でき、特に、アルカリ水による洗
顔及び酸性水によるトリートメントを113続的に行う
のに好都合である。
Therefore, it can be used for many purposes, and is particularly convenient for continuously performing facial cleansing with alkaline water and treatment with acidic water.

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

第1図は本発明の一実施例による電解整水装置の概略構
成図、 第2図は本発明の他の実施例による電解整水装
置の概略構成図である。 1′・・・電解槽、 2.3・・・電極、 4・・・電
解隔膜、 5・・・給水管路、 6,7・・・排水管路
、 8・・・取水管路、 9,10・・・中和剤供給回
路、  II・・・選択開閉バルブ装置、  12.1
3・・・中和剤タンク、  16・・流量比調整バルブ
、  l 7−極性切換制御部、  18・・・流路切
換バルブ。 特許出願人    岡 崎 龍 夫 代理人    弁理士性 藤 直 義
FIG. 1 is a schematic diagram of an electrolytic water conditioning device according to one embodiment of the present invention, and FIG. 2 is a schematic diagram of an electrolytic water conditioning device according to another embodiment of the present invention. 1'... Electrolytic cell, 2.3... Electrode, 4... Electrolytic diaphragm, 5... Water supply pipe, 6, 7... Drainage pipe, 8... Water intake pipe, 9 , 10... Neutralizing agent supply circuit, II... Selective opening/closing valve device, 12.1
3... Neutralizing agent tank, 16... Flow ratio adjustment valve, l 7-Polarity switching control section, 18... Flow path switching valve. Patent applicant Tatsuo Okazaki Agent Patent attorney Naoyoshi Fuji

Claims (4)

【特許請求の範囲】[Claims] (1)極性の異なる一対の電極間を電解隔膜によって一
対の電極室に区画した電解槽を具備し、この電解槽の一
側に給水管路を設けるとともに、他側に、前記各々の電
極室に連通する一対の電解水排水管路を合流させて排出
する電解水取水管路を設けた水の電解装置と、 電解槽の陰極室に酸性中和剤を供給し、陽極室にアルカ
リ中和剤を供給する二系統の中和剤供給回路と、 二系統の中和剤供給回路の途中に設けられ、これら二系
統の中和剤供給回路を選択的に開閉するバルブ装置とを
具備することを特徴とする電解整水装置。
(1) Equipped with an electrolytic cell in which a pair of electrodes with different polarities are divided into a pair of electrode chambers by an electrolytic diaphragm, a water supply pipe is provided on one side of the electrolytic cell, and each of the electrode chambers is provided on the other side. A water electrolysis device is equipped with an electrolyzed water intake pipe that merges and discharges a pair of electrolyzed water drainage pipes that communicate with and a valve device provided in the middle of the two neutralizing agent supply circuits to selectively open and close these two neutralizing agent supply circuits. An electrolytic water conditioning device featuring:
(2)電解装置の一対の電極を印加電圧の極性を切り換
えて連続的に電解できる陰極・陽極両用の電極で構成す
るとともに、電解装置の電源回路に電圧極性切換制御部
を具備し、さらに、前記二系統の中和剤供給管路に前記
電圧極性切換制御部の作動に連動してこれら二系統の中
和剤供給管路の流路を切換える切換バルブを具備してい
ることをさらに特徴とする請求項(1)記載の電解整水
装置。
(2) The pair of electrodes of the electrolyzer is configured with a cathode/anode electrode that can perform continuous electrolysis by switching the polarity of the applied voltage, and the power supply circuit of the electrolyzer is equipped with a voltage polarity switching control section, and It is further characterized in that the two systems of neutralizing agent supply conduits are provided with a switching valve that switches the flow paths of these two systems of neutralizing agent supply conduits in conjunction with the operation of the voltage polarity switching control section. The electrolytic water conditioning device according to claim (1).
(3)電解装置の一対の電解水排水管路に流量比調整バ
ルブを設けたことを特徴とする請求項(2)または(3
)記載の電解整水装置。
(3) Claim (2) or (3) characterized in that a flow ratio adjustment valve is provided in a pair of electrolyzed water drainage pipes of the electrolyzer.
) described electrolytic water conditioning device.
(4)電解装置の一対の電解水排水管路に、電圧極性切
換制御部の切り換えに連動して該一対の電解水排水流量
を所定流量比に調整する流量比調整バルブを設けたこと
を特徴とする請求項(2)記載の電解整水装置。
(4) The pair of electrolyzed water drainage pipes of the electrolyzer are provided with a flow ratio adjustment valve that adjusts the pair of electrolyzed water drainage flow rates to a predetermined flow ratio in conjunction with switching of the voltage polarity switching control unit. The electrolytic water conditioning device according to claim (2).
JP2213282A 1990-08-10 1990-08-10 Electrolyzed water straightening equipment Pending JPH0499295A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2213282A JPH0499295A (en) 1990-08-10 1990-08-10 Electrolyzed water straightening equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2213282A JPH0499295A (en) 1990-08-10 1990-08-10 Electrolyzed water straightening equipment

Publications (1)

Publication Number Publication Date
JPH0499295A true JPH0499295A (en) 1992-03-31

Family

ID=16636530

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2213282A Pending JPH0499295A (en) 1990-08-10 1990-08-10 Electrolyzed water straightening equipment

Country Status (1)

Country Link
JP (1) JPH0499295A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6217741B1 (en) 1998-10-13 2001-04-17 Morinaga Engineering Co., Ltd. Method for manufacturing bactericide

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6217741B1 (en) 1998-10-13 2001-04-17 Morinaga Engineering Co., Ltd. Method for manufacturing bactericide

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