JPH0751672A - Method for electrolytically treating water - Google Patents
Method for electrolytically treating waterInfo
- Publication number
- JPH0751672A JPH0751672A JP22058493A JP22058493A JPH0751672A JP H0751672 A JPH0751672 A JP H0751672A JP 22058493 A JP22058493 A JP 22058493A JP 22058493 A JP22058493 A JP 22058493A JP H0751672 A JPH0751672 A JP H0751672A
- Authority
- JP
- Japan
- Prior art keywords
- water
- electrolytic
- polarity
- chamber
- electrode
- 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
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Description
【0001】[0001]
【発明の利用分野】本発明は有隔膜電解槽で水を電解
し、使用目的に応じて飲用のアルカリイオン水や酸性電
解殺菌水を生成する電解整水方法の改良に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrolytic water conditioning method for electrolyzing water in a diaphragm electrolyzer to produce alkaline ionized water for drinking or acidic electrolytic sterilized water according to the purpose of use.
【0002】[0002]
【従来の技術】電解隔膜で仕切られた一対の+−電極室
の水に電解電圧を印加し、目的に応じて陰極室からアル
カリイオン水を得、あるいは、陽極室から殺菌水を得る
電解整水方法が知られている。この場合、同じ極性で長
時間電解すると、陰極などのアルカリ水系路にカルシウ
ムなどの折出物が付着し、電解効率を低下させてしま
う。このため、所定時間毎に両電極に印加する電圧の極
性を切換えて電解整水を行うことにより、目的の電解水
を生成しながら折出カルシウムを水に溶解させる方法が
とられている。2. Description of the Related Art An electrolytic voltage is applied to water in a pair of positive and negative electrode chambers partitioned by electrolytic diaphragms to obtain alkaline ionized water from the cathode chamber or sterilized water from the anode chamber according to the purpose. Water methods are known. In this case, if electrolysis is performed with the same polarity for a long time, a protrusion such as calcium adheres to an alkaline water channel such as a cathode, which lowers the electrolysis efficiency. Therefore, a method is adopted in which the polarity of the voltage applied to both electrodes is switched every predetermined time to carry out electrolytic water conditioning to dissolve the precipitated calcium in water while generating the target electrolyzed water.
【0003】[0003]
【発明が解決しようとする課題】ところで、有隔膜電解
槽では目的の電解水を生成する場合、陰極室と陽極室の
流量比率が異なる。例えば、アルカリ水を目的とする場
合の流量比はアルカリ水側(陰極室)2に対し、酸性水
側(陽極室)1であり、酸性水側での殺菌水の生成を目
的とする場合の流量比は例えばアルカリ水側1に対し、
酸性水側2である。 また、円筒型電解槽を隔膜によっ
て一対の同心形電極室に仕切った連続通水式の電解整水
装置は、内側電極と外側電極の電極表面積が異なり、さ
らに、内側電極室と外側電極室の水通路の横断面積及び
流速が異なる。By the way, in the diaphragm membrane electrolytic cell, when the target electrolyzed water is produced, the flow rate ratio between the cathode chamber and the anode chamber is different. For example, the flow rate ratio for the purpose of alkaline water is to the alkaline water side (cathode chamber) 2 to the acidic water side (anode chamber) 1, and for the purpose of producing sterile water on the acidic water side. The flow rate ratio is, for example, 1 for alkaline water side,
Acidic water side 2. Further, the continuous water flow type electrolytic water conditioner in which the cylindrical electrolytic cell is partitioned into a pair of concentric electrode chambers by a diaphragm has different electrode surface areas of the inner electrode and the outer electrode, and further, the inner electrode chamber and the outer electrode chamber. The cross-sectional area of the water passage and the flow velocity are different.
【0004】このように、電極表面、電極室の断面積あ
るいは流速の違いにより一対の電極室の電解効率が異な
る電極槽を使用し、電極の極性を所定時間毎に切り換え
て連続的に電解整水をしようとすると、極性の切換え、
すなわち電極室の相互入れ換えによって使用目的の電解
水のpHが必然的に変化してしまい、pHの均一な電解
水が得られないという問題が生ずる。As described above, an electrode tank is used in which the electrolysis efficiency of the pair of electrode chambers differs depending on the difference in the electrode surface, the cross-sectional area of the electrode chambers, or the flow velocity, and the polarity of the electrodes is switched at predetermined intervals to continuously perform electrolytic preparation. When trying to water, switch the polarity,
That is, the pH of the electrolyzed water to be used inevitably changes due to the mutual exchange of the electrode chambers, which causes a problem that electrolyzed water having a uniform pH cannot be obtained.
【0005】本発明の目的は、所定の時間毎に電極の極
性を逆転して電解整水を行う有隔膜の電解水処理におい
て、極性変換による使用目的の水のpH変化を少なく
し、pHの均一性を保持もしくは助長することにある。An object of the present invention is to reduce the pH change of water for use due to polarity change in the electrolyzed water treatment of a diaphragm in which the polarity of electrodes is reversed every predetermined time to perform electrolytic water conditioning. To maintain or promote uniformity.
【0008】[0008]
【実施例】図1は電解整水装置の1例を示すもので、こ
の装置の電解槽1は、内側電極2と外側電極3を同心状
に配し、両電極2、3間を電解隔膜4によって内側電極
室5と外側電極室6に仕切った構成になり、給水部7か
ら原水を導入しながら両電極2、3に直流の電解電圧を
印加することによって水を電解し、陰極室に生成される
アルカリ水と陽極室に生成される酸性水を各別の電解水
排水管8、9から排出するようになっている。EXAMPLE FIG. 1 shows an example of an electrolytic water conditioning apparatus. An electrolytic cell 1 of this apparatus has an inner electrode 2 and an outer electrode 3 arranged concentrically, and an electrolytic diaphragm between both electrodes 2 and 3. 4 is divided into an inner electrode chamber 5 and an outer electrode chamber 6, and while introducing raw water from the water supply section 7, water is electrolyzed by applying a direct current electrolysis voltage to both electrodes 2 and 3 to form a cathode chamber. The generated alkaline water and the acidic water generated in the anode chamber are discharged from the separate electrolyzed water drain pipes 8 and 9.
【0009】両電極2、3に電解電圧を印加する電気回
路10には、電気制御部11が設けられており、この制
御部11により内側電極2と外側電極3の極性を所定時
間毎に逆転して、陰極室側に折出するカルシウム等を極
性転換後の酸性水中に溶解させるようにしてある。An electric control unit 11 is provided in the electric circuit 10 for applying an electrolytic voltage to both electrodes 2 and 3, and the control unit 11 reverses the polarities of the inner electrode 2 and the outer electrode 3 at predetermined time intervals. Then, calcium or the like protruding to the cathode chamber side is dissolved in the acidic water after the polarity conversion.
【0010】ところで、この種の電解槽1は、内側電極
2、3の電解表面積が異なり、また、アルカリ水を目的
とする場合も、酸性水を目的とする場合も、陰極室と陽
極室の流量比あるいは流速が異なる。従って、同じ電圧
の電流を供給しながら電極の極性を転換すると、外側電
極室6と内側電極室5とで目的の電解水のpHは変わっ
てしまう。例えば、アルカリ水を目的とする場合、外側
電極3を陰極として所定pHのアルカリ水を得るように
基準電解電圧を設定した電解槽にあっては、電極の極性
転換により電解面積の小さい内側電極2が陰極に転換さ
れるとアルカリ水生成の電解効率が低下し、所定のpH
のアルカリ水が得られなくなる。この逆の場合、すなわ
ち、内側電極2を陰極として所定pHのアルカリ水を得
るように基準電解電圧を設定した場合は逆の現象が生
じ、いずれにしても、電流供給量を同じにしたままで電
解効率の異なる電極室の極性を転換するとpHの変動は
さけられない。By the way, in this type of electrolytic cell 1, the inner electrodes 2 and 3 have different electrolysis surface areas, and the cathode chamber and the anode chamber can be used for both alkaline water and acidic water. Flow rate or flow velocity is different. Therefore, if the polarities of the electrodes are changed while supplying the current of the same voltage, the pH of the target electrolyzed water will change between the outer electrode chamber 6 and the inner electrode chamber 5. For example, when alkaline water is intended, in an electrolytic cell in which a reference electrolysis voltage is set so that the outer electrode 3 serves as a cathode and alkaline water having a predetermined pH is obtained, the inner electrode 2 having a small electrolysis area due to the polarity change of the electrode. When is converted to a cathode, the electrolysis efficiency of alkaline water generation decreases, and
No alkaline water can be obtained. In the opposite case, that is, when the reference electrolysis voltage is set so that the inner electrode 2 is used as a cathode and alkaline water of a predetermined pH is obtained, the opposite phenomenon occurs, and in any case, the current supply amount remains the same. When the polarities of the electrode chambers having different electrolysis efficiencies are changed, the fluctuation of pH cannot be avoided.
【0011】そこで、本発明は、電極の極性転換に連動
して、印加電解電圧を、目的の電解水のpHの均一性が
助長される側に調整するようにしたものである。すなわ
ち、上記アルカリ水を目的とする実施例では、電極の極
性転換によりアルカリ水を生成する陰極室が外側電極室
6から内側電極室5に切換わると、陰極の電解面積が小
さくなることにより、アルカリ水の電解効率が低下して
pH値が下がるので電圧を上げ、電解電流が多く流れる
ようにする。こうすることにより、アルカリ水のpH値
低下が補正され、pHの均質性が得られる。他方、極性
の再転換により陰極室が内側電極室5から外側電極室6
へ切換わるとこれに連動して印加電圧を元に戻す。In view of this, the present invention adjusts the applied electrolysis voltage to the side where the uniformity of the pH of the target electrolyzed water is promoted in conjunction with the polarity change of the electrode. That is, in the above-mentioned embodiment for alkaline water, when the cathode chamber for generating alkaline water by switching the polarities of the electrodes is switched from the outer electrode chamber 6 to the inner electrode chamber 5, the electrolytic area of the cathode is reduced, Since the electrolysis efficiency of alkaline water is lowered and the pH value is lowered, the voltage is raised so that a large amount of electrolysis current flows. By doing so, the decrease in the pH value of the alkaline water is corrected, and the homogeneity of the pH is obtained. On the other hand, the cathode chamber is changed from the inner electrode chamber 5 to the outer electrode chamber 6 by re-polarization.
When is switched to, the applied voltage is returned to the original in conjunction with this.
【0012】かくして、電解槽の極性転換に伴って電解
電圧を調整することにより、極性が転換されても、pH
値が均一な目的の電解水が得られる。Thus, by adjusting the electrolysis voltage according to the polarity change of the electrolytic cell, even if the polarity is changed, the pH is changed.
The desired electrolyzed water having a uniform value can be obtained.
【0013】尚、極性転換に伴う電解電圧の調整は電気
回路10の電気制御部11に必要な回路を組込むことに
より、容易に実施が可能である。The adjustment of the electrolysis voltage due to the polarity change can be easily carried out by incorporating a necessary circuit in the electric control section 11 of the electric circuit 10.
【0014】上記は主としてアルカリイオン水を生成す
る場合について説明したが、陽極室側から酸性の電解殺
菌水を生成する場合にも同様に適用される。Although the above description has been made mainly for the case of producing alkaline ionized water, the same applies to the case of producing acidic electrolytic sterilized water from the anode chamber side.
【0015】また、上記説明は電極の電解表面積の違い
によって電極室の電解効率が変る場合について述べた
が、電極室の断面積、流速の違いにより電解効率が違う
場合についても同様に適用される。。Further, although the above description has described the case where the electrolysis efficiency of the electrode chamber changes depending on the difference in the electrolysis surface area of the electrode, the same applies to the case where the electrolysis efficiency varies depending on the cross-sectional area and flow velocity of the electrode chamber. . .
【0016】さらに、上記の説明では、円筒型の連続式
電解槽を使用する場合を例示したが、その他の電解槽、
例えばバッチ式電解槽を使用する場合にも同様に適用さ
れるものである。Further, in the above description, the case of using the cylindrical continuous type electrolytic cell is exemplified, but other electrolytic cells,
The same applies to the case of using a batch type electrolytic cell, for example.
【0017】[0017]
【効果】本発明は以上の構成により、電極の極性転換に
よりカルシウム折出の弊害をなくしながら、しかも極性
転換によりpH変動が補正されるので、品質の良いアル
カリイオン水あるいは酸性水(殺菌水)を効率良く生成
することができる。[Effects] With the above-described structure, the polarity change of the electrode eliminates the adverse effect of calcium protrusion, and the pH change is corrected by the polarity change. Therefore, high-quality alkaline ionized water or acidic water (sterilized water) is used. Can be efficiently generated.
【図1】 本発明の電解処理方法に使用される電解整水
装置の一例を示す概略構成図である。FIG. 1 is a schematic configuration diagram showing an example of an electrolytic water conditioning apparatus used in an electrolytic treatment method of the present invention.
1…電解槽、 2、3…電極、 4…電解隔膜、 5、
6…電極室、 8、9…電解水排出管、 10…電気回
路、11…電気制御部。1 ... Electrolyte tank, 2, 3 ... Electrode, 4 ... Electrolytic diaphragm, 5,
6 ... Electrode chamber, 8, 9 ... Electrolyzed water discharge pipe, 10 ... Electric circuit, 11 ... Electric control part.
Claims (1)
る電極室の断面積もしくは流速の違いによって、一対の
電極室の電解効率が異なる有隔膜電解槽を使用し、両電
極に印加する電解電圧の極性を所定時間毎に逆転して電
解整水を行う電解水処理方法において、電極の極性切換
えに際し、目的の電解水のpHの均一性を助長するよう
に電極の極性切換えに連動して電極への印加電流を調整
することを特徴とする水の電解処理方法1. An electrolytic voltage applied to both electrodes using a diaphragm electrolyzer in which the electrolysis efficiency of a pair of electrode chambers differs depending on the surface area of the opposing electrodes or the cross-sectional area or flow velocity of the opposing electrode chambers. In the electrolyzed water treatment method in which the polarity is reversed every predetermined time to perform electrolytic water conditioning, when the polarity of the electrode is switched, the polarity of the electrode is switched so as to promote the uniformity of the pH of the target electrolyzed water. Method of electrolytic treatment of water characterized by adjusting current applied to
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22058493A JPH0751672A (en) | 1993-08-12 | 1993-08-12 | Method for electrolytically treating water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22058493A JPH0751672A (en) | 1993-08-12 | 1993-08-12 | Method for electrolytically treating water |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0751672A true JPH0751672A (en) | 1995-02-28 |
Family
ID=16753265
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22058493A Pending JPH0751672A (en) | 1993-08-12 | 1993-08-12 | Method for electrolytically treating water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0751672A (en) |
-
1993
- 1993-08-12 JP JP22058493A patent/JPH0751672A/en active Pending
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