JP3820248B2 - Electrolytic water conditioner - Google Patents

Electrolytic water conditioner Download PDF

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JP3820248B2
JP3820248B2 JP2003540090A JP2003540090A JP3820248B2 JP 3820248 B2 JP3820248 B2 JP 3820248B2 JP 2003540090 A JP2003540090 A JP 2003540090A JP 2003540090 A JP2003540090 A JP 2003540090A JP 3820248 B2 JP3820248 B2 JP 3820248B2
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カン，ソンシク
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    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104—Devices therefor; Their operating or servicing
    • C02F1/4618—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104—Devices therefor; Their operating or servicing
    • C02F1/4618—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water
    • C02F2001/4619—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water only cathodic or alkaline water, e.g. for reducing
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/02—Non-contaminated water, e.g. for industrial water supply
    • C02F2103/026—Treating water for medical or cosmetic purposes
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00—Apparatus for treatment of water, waste water or sewage
    • C02F2201/46—Apparatus for electrochemical processes
    • C02F2201/461—Electrolysis apparatus
    • C02F2201/46105—Details relating to the electrolytic devices
    • C02F2201/4611—Fluid flow
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00—Apparatus for treatment of water, waste water or sewage
    • C02F2201/46—Apparatus for electrochemical processes
    • C02F2201/461—Electrolysis apparatus
    • C02F2201/46105—Details relating to the electrolytic devices
    • C02F2201/46115—Electrolytic cell with membranes or diaphragms
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/04—Oxidation reduction potential [ORP]
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/06—Controlling or monitoring parameters in water treatment pH
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00—Specific treatment goals
    • C02F2303/04—Disinfection

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Description

本発明は、水を２回電気分解して強アルカリ水、活性水素の豊富な弱アルカリ水および酸性水の３種類の水を、流入水の水質と関係なく提供できるようにした電気分解整水器に関する。   The present invention electrolyzes water twice to provide three types of water, strong alkaline water, weak alkaline water rich in active hydrogen, and acidic water, regardless of the quality of the influent water. Related to the vessel.

さまざまな病気の原因とされる「活性酸素」とは、活性のある酸素、すなわち酸化作用が特に強い酸素のことであるが、このような特に強い活性酸素の酸化作用によって人体の細胞や遺伝子を酸化させて各種疾病を引き起こす原因となる。   “Active oxygen”, which is the cause of various diseases, is active oxygen, that is, oxygen that has a particularly strong oxidative action. Oxidizes and causes various diseases.

ところが、私たちが摂取する食べ物が酸素によって酸化されて生命を維持するのに必要な物質やエネルギーを作り出す一方、酸素は食べ物によって還元されて「活性酸素」になるので、この活性酸素は体内で絶えず発生している。   However, the food we consume is oxidized by oxygen to produce substances and energy necessary to maintain life, while oxygen is reduced by food to become “active oxygen”, so this active oxygen is absorbed by the body. It is constantly occurring.

よって、体内で絶えず発生している「活性酸素」を除去するためには還元作用に優れた「活性水素」を体内に十分提供する必要があり、この「活性水素」は水の電気分解によって得られるアルカリ水から得ることができる。   Therefore, in order to remove “active oxygen” that is constantly generated in the body, it is necessary to provide the body with “active hydrogen” that is excellent in reducing action. This “active hydrogen” is obtained by electrolysis of water. Can be obtained from alkaline water.

そこで、水を電気分解して飲用が可能なｐＨ７．４〜８．５の弱アルカリ水を飲料水として提供できるような整水器が導入された。このような整水器の通常の構造は浄水部と電解部とから構成されており、電気分解が起こる電解部には、１つの陽極電極板１と２つの陰極電極板２及び３とが、水に含まれているイオンのみが移動できるような２つの隔膜４，５の間に設置されて３つの電極室を構成することにより、２つの陰極電極室からは強アルカリ水（ｐＨ９〜１０）および弱アルカリ水（ｐＨ７．４〜８．５）を生成する一方、陽極電極室からは酸性水（ｐＨ４〜５）の電解イオン水を生成するようになっている。このうち、飲用可能な弱アルカリ水を飲料水として用いる。   Therefore, a water conditioner has been introduced that can provide weak alkaline water having a pH of 7.4 to 8.5 that can be electrolyzed and drinkable as drinking water. The normal structure of such a water conditioner is composed of a water purification unit and an electrolysis unit, and in the electrolysis unit where electrolysis occurs, one anode electrode plate 1 and two cathode electrode plates 2 and 3 are provided. By constructing three electrode chambers between two diaphragms 4 and 5 so that only ions contained in water can move, strong alkaline water (pH 9 to 10) is generated from the two cathode electrode chambers. In addition, weak alkaline water (pH 7.4 to 8.5) is generated, while electrolytic water of acidic water (pH 4 to 5) is generated from the anode electrode chamber. Among these, drinkable weak alkaline water is used as drinking water.

このような反応は水の電気分解過程において、塩素、硫酸、硫黄などの陰イオンは、陽極電極板１へ移動して陽極電解水と一緒に排出されるとともに、水酸イオン（OH-）が陽極に電子（e-）を奪われて酸化反応が起こり酸素分子（O2）になるので、この際に排出される陽極電解水は、水素イオン濃度が上昇するために酸性になる。 In such an electrolysis process, anions such as chlorine, sulfuric acid, and sulfur move to the anode electrode plate 1 and are discharged together with the anode electrolyzed water, and hydroxide ions (OH-) are generated. Electrons (e-) are taken away from the anode and an oxidation reaction takes place, resulting in oxygen molecules (O 2 ). The anodic electrolyzed water discharged at this time becomes acidic because the hydrogen ion concentration increases.

一方、水に含まれているカルシウム、マグネシウム、カリウムなどのミネラル成分である陽イオンは、陰極電極板２，３へ移動して放電された後、水に再び溶解されて陰極電解水と一緒に排出されるとともに、水素イオン（H+）が陰極から電子（e-）を受け取って「活性水素」を生成するので、この際に排出される陰極電解水は水素イオン（H+）濃度が一般的な水よりも低下してしまうためにアルカリ性となり、酸化還元電位も低くなる。 On the other hand, cations, which are mineral components such as calcium, magnesium and potassium, contained in water move to the cathode electrode plates 2 and 3 and are discharged, and then are dissolved again in water and together with the cathode electrolyzed water. As it is discharged, hydrogen ions (H + ) receive electrons (e-) from the cathode and generate “active hydrogen”, so the cathode electrolyzed water discharged at this time generally has a hydrogen ion (H + ) concentration As a result, it becomes alkaline and the oxidation-reduction potential is lowered.

しかし、このような構造の従来の整水器は、３種類の電解イオン水（強アルカリ水、弱アルカリ水、酸性水）を生成するに際して、水を１回だけ電気分解するので、流入する水の性質によって陰極付近の水素イオンの濃度が一定ではなく、陽イオンが十分除去されず、さらに酸化還元電位の低下を図り難いため、「活性水素」の豊富な弱アルカリ水を安定的に得ることができないという問題点があった。   However, the conventional water conditioner having such a structure electrolyzes water only once when generating three types of electrolytic ionic water (strong alkaline water, weak alkaline water, and acidic water). The concentration of hydrogen ions in the vicinity of the cathode is not constant due to the nature of the cation, the cations are not sufficiently removed, and it is difficult to lower the oxidation-reduction potential, so it is possible to stably obtain weak alkaline water rich in "active hydrogen" There was a problem that could not.

（発明の概要）
本発明は、かかる従来の問題点を解決するために案出されたもので、その目的は、流入水の水質に関係なく「活性水素」の豊富な弱アルカリ水を安定的に得ることができる整水器を提供することにある。 (Summary of Invention)
The present invention has been devised to solve such conventional problems, and its purpose is to stably obtain weak alkaline water rich in “active hydrogen” regardless of the quality of the influent water. The purpose is to provide a water conditioner.

上記目的を達成するために、本発明の整水器は、それぞれ相異なる２つの電解部を備え、陽極および陰極で構成された１次電解部では２つの電極室でアルカリ水と酸性水とに電気分解した後、１次電解部で生成されたアルカリ水を陽極、陰極および陰極で構成された２次電解部で再び電気分解して、「活性水素」のより豊富な弱アルカリ水を飲料水として提供し、それに加えて洗浄用強アルカリ水と、洗顔用酸性水とを提供することを特徴とする。   In order to achieve the above object, the water conditioner of the present invention includes two electrolysis parts different from each other. In the primary electrolysis part composed of an anode and a cathode, alkaline water and acid water are used in two electrode chambers. After the electrolysis, the alkaline water produced in the primary electrolysis unit is electrolyzed again in the secondary electrolysis unit composed of an anode, a cathode and a cathode, and weak alkaline water richer in “active hydrogen” is consumed as drinking water. In addition to the above, strong alkaline water for washing and acidic water for facial washing are provided.

（図面の簡単な説明）
図１は、本発明の整水器の構造を示す断面図である。
図２は、本発明の整水器の１次電解部を示す部分断面図である。
図３は、本発明の整水器の２次電解部を示す部分断面図である。
図４は、本発明の整水器の他の構造を示す断面図である。
図５は、本発明の整水器の電解イオン水の生成過程を示す流れ図である。
図６は、従来の整水器の構造を示す断面図である。 (Brief description of the drawings)
FIG. 1 is a cross-sectional view showing the structure of the water conditioner of the present invention.
FIG. 2 is a partial cross-sectional view showing the primary electrolysis unit of the water adjuster of the present invention.
FIG. 3 is a partial cross-sectional view showing a secondary electrolysis unit of the water adjuster of the present invention.
FIG. 4 is a cross-sectional view showing another structure of the water adjuster of the present invention.
FIG. 5 is a flowchart showing the process of generating electrolytic ionic water in the water conditioner of the present invention.
FIG. 6 is a cross-sectional view showing the structure of a conventional water conditioner.

以下、添付図を参照して本発明の最適な一実施例を詳細に説明する。   Hereinafter, an exemplary embodiment of the present invention will be described in detail with reference to the accompanying drawings.

図１は本発明の一実施例を示す断面図であって、水を電気分解して電解イオン水を生成するための電解部と、水中の異物や有機物、さび、塩素、匂いなどを除去するための浄水部とから構成される通常の電気分解整水器において、前記電解部に、アルカリ水および酸性水を生成するための１次電解部１０と、１次電解部１０で生成されたアルカリ水を再び電気分解して強アルカリ水、弱アルカリ水および酸性水を生成するための２次電解部２０とを構成したものである。   FIG. 1 is a cross-sectional view showing an embodiment of the present invention, in which an electrolysis unit for electrolyzing water to generate electrolytic ionic water, and removing foreign matter, organic matter, rust, chlorine, odor, etc. in the water. In the normal electrolysis water regulating apparatus comprised from the water purification part for the primary electrolysis part 10 for producing | generating alkaline water and acidic water in the said electrolysis part, and the alkali produced | generated by the primary electrolysis part 10 The secondary electrolysis part 20 for electrolyzing water again and producing | generating strong alkaline water, weak alkaline water, and acidic water is comprised.

この際、前記電解部の１次電解部１０には、それぞれ１つの＋電極板（陽極）１１と−電極板（陰極）１２とが設置され、その間に水に含まれたイオンのみが通過し得るイオン分離隔膜１４が設置されることで２つの電極室が形成される一方、２次電解部２０には、１つの＋電極板（陽極）２１と２つの−電極板（陰極）２２，２３が設置され、前記電極板２１，２２，２３の間に２つの隔膜２４，２５が設置されることで３つの電極室が形成される。   At this time, one positive electrode plate (anode) 11 and one negative electrode plate (cathode) 12 are installed in the primary electrolysis unit 10 of the electrolysis unit, and only ions contained in water pass between them. Two electrode chambers are formed by installing the ion separation diaphragm 14 to be obtained, while the secondary electrolysis unit 20 includes one + electrode plate (anode) 21 and two − electrode plates (cathode) 22 and 23. Is installed, and two diaphragms 24 and 25 are installed between the electrode plates 21, 22 and 23 to form three electrode chambers.

また、前記浄水部には、流入水の異物や有機物、さび、塩素、匂いなどの除去に用いられる種々のフィルター３０が装着される。前記浄水部は前記電解部１の前端に設置され、電気分解の前に予め行われる水の浄水に使用されるが、後端に設置しても、または必要に応じて前端および後端の両方に設置しても良い。   The water purification unit is equipped with various filters 30 used for removing foreign substances, organic substances, rust, chlorine, odors, and the like of influent water. The water purification unit is installed at the front end of the electrolysis unit 1 and is used for water purification performed in advance before electrolysis, but even if installed at the rear end, or both the front end and the rear end as necessary. It may be installed in.

次に、本発明の電気分解整水器から得られる電解イオン水の生成過程を説明する。   Next, the production process of electrolytic ionic water obtained from the electrolyzed water conditioner of the present invention will be described.

先ず、浄水部２で浄水した水が１次電解部１０の流入口１６を通して１次電解部１０へ流入すると、＋電極板１１および−電極板１２に電源が供給され、これにより＋電極板１１と隔膜１４との間の第１電極室では酸性水が生成されて酸性水排出口１７へ排出され、また、隔膜１４と−電極板１２との間の第２電極室ではアルカリ水が生成されて２次電解部２０の流入口１８へ排出される。   First, when the water purified by the water purification unit 2 flows into the primary electrolysis unit 10 through the inlet 16 of the primary electrolysis unit 10, power is supplied to the + electrode plate 11 and the − electrode plate 12, thereby the + electrode plate 11. Acid water is generated in the first electrode chamber between the diaphragm 14 and the diaphragm 14 and discharged to the acidic water discharge port 17, and alkaline water is generated in the second electrode chamber between the diaphragm 14 and the negative electrode plate 12. And discharged to the inlet 18 of the secondary electrolysis unit 20.

その後、アルカリ水が２次電解部２０の流入口１８へ流入すると、＋電極板２１および−電極板２２，２３に電源が供給され、これにより＋電極板２１と隔膜２４との間では酸性水が生成され、前記１次電解部１０から生成された酸性水と合流して洗顔水排出口２７へ排出され、また、隔膜２４と−電極板２２との間、および電極板２２と隔膜２５との間では強アルカリ水が生成され、洗浄水排出口２８へ排出され、さらに、隔膜２５と−電極板２３との間の第３電極室では弱アルカリ水が生成されて飲料水排出口２９へ排出される。   Thereafter, when alkaline water flows into the inlet 18 of the secondary electrolysis unit 20, power is supplied to the + electrode plate 21 and the − electrode plates 22, 23, whereby acid water is provided between the + electrode plate 21 and the diaphragm 24. Is generated and merged with the acidic water generated from the primary electrolysis unit 10 and discharged to the face-washing water outlet 27, and between the diaphragm 24 and the electrode plate 22, and between the electrode plate 22 and the diaphragm 25. Strong alkaline water is generated between the two, and is discharged to the washing water discharge port 28. Further, weak alkaline water is generated in the third electrode chamber between the diaphragm 25 and the negative electrode plate 23 to the drinking water discharge port 29. Discharged.

この時、前記３つの電解イオン水（強アルカリ水、弱アルカリ水、酸性水）は次のようにそれぞれ相異なる作用効果を奏する。   At this time, the three electrolytic ionic waters (strong alkaline water, weak alkaline water, and acidic water) have different effects as follows.

先ず、１次電解部１０の＋電極板１１が含まれた第１電極室には、水に含有されている塩素、硫酸、硫黄などの陰イオンが集まり、水酸イオン（OH-）が＋電極板１１に電子（e-）を奪われて酸化反応が起こり酸素分子O2になるため、水素イオン濃度が上昇して酸性の水になり、この酸性水は殺菌および皮膚収斂効果を有するようになるので、洗顔用として用いることができる。 First, in the first electrode chamber including the + electrode plate 11 of the primary electrolysis unit 10, anions such as chlorine, sulfuric acid, and sulfur contained in water gather and hydroxide ions (OH−) are + Electrons (e-) are taken away by the electrode plate 11 and become an oxygen molecule O 2 , so that the hydrogen ion concentration increases to become acidic water, and this acidic water seems to have a bactericidal and skin convergence effect. Therefore, it can be used for face washing.

また、１次電解部１０の−電極板１２が含まれた第２電極室には、水に含有されているカルシウム、マグネシウム、カリウムなどのミネラル成分である陽イオンが集まり、水素イオン（H+）が＋電極板１２から電子（e-）を受け取って「活性水素」が生成され、水素イオン（H+）の濃度が低下してアルカリ性の水になり、また酸化還元電位（ORP）が低くなって、水の殺菌用として使用することができる。 Further, in the second electrode chamber including the negative electrode plate 12 of the primary electrolysis unit 10, cations that are mineral components such as calcium, magnesium, and potassium contained in water gather, and hydrogen ions (H + ) Receives electrons (e−) from the + electrode plate 12 to generate “active hydrogen”, the concentration of hydrogen ions (H + ) decreases to alkaline water, and the redox potential (ORP) is low. It can be used for water sterilization.

この際、第２電極室で生成されて「活性水素」が含まれたアルカリ水は２次電解部２０へ送られ、＋電極板２１と遠距離の−電極板２３が含まれた第３電極室には、水に含有されているカルシウム、マグネシウム、カリウムなどのミネラル成分である陽イオンが集まり、水素イオン（H+）が−電極板２３から電子（e-）を受け取って「活性水素」がさらに生成されることにより、前記第２電極室よりも多量の「活性水素」が得られることはもとより、酸化還元電位（ORP）がより低くなり、水素イオン（H+）の濃度がｐＨ７．４〜８．５ほどの弱アルカリ性の水となって、飲料水として用いることができる。 At this time, the alkaline water generated in the second electrode chamber and containing “active hydrogen” is sent to the secondary electrolysis unit 20, and the third electrode including the + electrode plate 21 and the long-distance -electrode plate 23 is included. In the chamber, cations that are mineral components such as calcium, magnesium, and potassium contained in water gather, and hydrogen ions (H + ) receive electrons (e−) from the electrode plate 23 to become “active hydrogen”. Is further generated, so that a larger amount of “active hydrogen” is obtained than in the second electrode chamber, and the oxidation-reduction potential (ORP) is lower and the concentration of hydrogen ions (H + ) is pH 7. It becomes weak alkaline water of about 4 to 8.5 and can be used as drinking water.

また、＋電極板２１と近距離の−電極板２２が含まれた第４電極室には、水に含有されているカルシウム、マグネシウム、カリウムなどのミネラル成分である陽イオンが集まり、水素イオン（H+）が−電極板２２から電子（e-）を受け取って「活性水素」をまたさらに生成されることにより、前記第２電極室よりも多量の「活性水素」が得られることはもとより、酸化還元電位（ORP）がより低くなり、殺菌効果を持つ、水素イオン（H+）の濃度がｐＨ９〜１０ほどの強アルカリ性の水になって、洗浄用として用いることができる。 In addition, in the fourth electrode chamber including the + electrode plate 21 and the − electrode plate 22 at a short distance, cations that are mineral components such as calcium, magnesium, and potassium contained in water gather, and hydrogen ions ( H + ) receives electrons (e−) from the − electrode plate 22 and further generates “active hydrogen”, so that a larger amount of “active hydrogen” than the second electrode chamber can be obtained. The oxidation-reduction potential (ORP) becomes lower and the concentration of hydrogen ions (H + ) having a bactericidal effect becomes strong alkaline water having a pH of about 9 to 10, and can be used for washing.

また、＋電極板２１が含まれた第５電極室には、前記第１電極室と同一の反応によって酸性水が生成されることにより、第１電極室から生成された酸性水と合流して洗浄用として用いることができる。   In addition, in the fifth electrode chamber including the + electrode plate 21, acid water is generated by the same reaction as the first electrode chamber, so that the acid water generated from the first electrode chamber is joined. It can be used for washing.

したがって、整水器は、１次電解部１０内で電気分解によって生成されたアルカリ水と酸性水とのうち２次電解部への流入水としてアルカリ水のみを使用し、２次電解部内で流入水の水質を整えることにより、活性水素と、カルシウム、カリウムおよびマグネシウムのようなミネラル陽イオンが豊富に含有された弱アルカリ水とを提供する。
そこで、飲用水としての弱アルカリ水は活性水素およびミネラル陽イオンを多量含有するので、体内で生成されて人体に悪影響を及ぼす活性酸素を除去することができる。
１次電解部１０内で生成される強アルカリ水は洗浄用として用い、酸性水は洗顔用として用いることができる。 Therefore, the water conditioner uses only alkaline water as inflow water to the secondary electrolysis part among alkaline water and acidic water generated by electrolysis in the primary electrolysis part 10 and flows into the secondary electrolysis part. By adjusting the quality of the water, active hydrogen and weakly alkaline water rich in mineral cations such as calcium, potassium and magnesium are provided.
Therefore, since weak alkaline water as drinking water contains a large amount of active hydrogen and mineral cations, it is possible to remove active oxygen produced in the body and adversely affecting the human body.
Strong alkaline water generated in the primary electrolysis unit 10 can be used for washing, and acidic water can be used for washing the face.

また、電気分解を２回行うことにより、２回の殺菌作用によって浄水効果をより向上させることができる。   Moreover, by performing electrolysis twice, the water purification effect can be further improved by two sterilization actions.

一方、図４は本発明の他の構造を示す図であって、前記１次電解部１０に隔膜１３をさらに設置して＋電極板１１と−電極板１２との間に２つの隔膜１３，１４を位置させ、この隔膜１３，１４の間に流出する中性水を２次電解部２０の流入口１８へ流入させて２次電気分解を行うようにしたもので、高硬度の水を本発明の整水器の流入水として使用する必要がある地域への適用を目的としたものであり、前記＋電極板１１および−電極板１２は一定周期で極性を転換させねばならないことは言うまでもない。   On the other hand, FIG. 4 is a diagram showing another structure of the present invention, in which a diaphragm 13 is further installed in the primary electrolysis unit 10 and two diaphragms 13, 14, and neutral water flowing between the diaphragms 13 and 14 flows into the inlet 18 of the secondary electrolysis unit 20 to perform secondary electrolysis. It is intended for application to an area that needs to be used as inflow water of the water conditioner of the invention, and it goes without saying that the polarity of the + electrode plate 11 and the −electrode plate 12 must be changed at a constant period. .

というのは、流入水が硬水である場合は、水に含まれている多量のイオン物質が前記＋電極板１１および−電極板にくっついて被覆するようになるため、過電流で電解作用が停止してしまうので、本発明の整水器の作動を阻害するからである。   This is because when the inflowing water is hard water, a large amount of ionic substances contained in the water adhere to and cover the + electrode plate 11 and the −electrode plate. This is because the operation of the water conditioner of the present invention is hindered.

この際、前記隔膜１４を設置するに代えて、整水器の流入口１６にイオン交換樹脂の充填されたイオン交換部を設置する場合にも、硬水を流入水として使用しうる同一の効果を得ることができる。   At this time, in place of installing the diaphragm 14, the same effect that hard water can be used as inflow water is also provided when an ion exchange part filled with ion exchange resin is installed at the inlet 16 of the water conditioner. Obtainable.

本発明の整水器の構造を示す断面図である。It is sectional drawing which shows the structure of the water adjuster of this invention. 本発明の整水器の１次電解部を示す部分断面図である。It is a fragmentary sectional view which shows the primary electrolysis part of the water adjuster of this invention. 本発明の整水器の２次電解部を示す部分断面図である。It is a fragmentary sectional view which shows the secondary electrolysis part of the water adjuster of this invention. 本発明の整水器の他の構造を示す断面図である。It is sectional drawing which shows the other structure of the water adjuster of this invention. 本発明の整水器の電解イオン水の生成過程を示す流れ図である。It is a flowchart which shows the production | generation process of the electrolytic ion water of the water adjuster of this invention. 従来の整水器の構造を示す断面図である。It is sectional drawing which shows the structure of the conventional water adjuster.

符号の説明Explanation of symbols

１０ １次電解部
１１ ＋電極板（陽極）
１２ −電極板（陰極）
１４ 隔膜
１６ 流入口
１７ 酸性水排出口
１８ 流入口
２０ ２次電解部
２１ ＋電極板（陽極）
２２ −電極板（陰極）
２３ −電極板（陰極）
２４ 隔膜
２５ 隔膜
２７ 洗顔水排出口
２８ 洗浄水排出口
２９ 飲料水排出口
３０ フィルター 10 Primary electrolysis part 11 + Electrode plate (anode)
12-Electrode plate (cathode)
14 Diaphragm 16 Inlet 17 Acidic water outlet 18 Inlet 20 Secondary electrolysis part 21 + Electrode plate (anode)
22-Electrode plate (cathode)
23-Electrode plate (cathode)
24 Diaphragm 25 Diaphragm 27 Face Wash Water Drain 28 Wash Water Drain 29 Drinking Water Drain 30 Filter

Claims (5)

電解部と浄水部とから構成される通常の電気分解整水器において、
前記電解部の流入口へ流入する水をアルカリ水と酸性水とに分離するために１つの＋電極板および−電極板を設置した電極室が、イオン分離隔膜によって２つの電極室に分けられた１次電解部と、
前記１次電解部で生成されたアルカリ水のみを流入させて３つの電解イオン水である飲用の高濃度の活性水素を有する弱アルカリ水と洗浄用強アルカリ水と洗顔用酸性水とに分離するために１つの＋電極板および２つの−電極板を設置した電極室が、２つのイオン分離隔膜によって３つの電極室に分けられた２次電解部とから構成されたことを特徴とする電気分解整水器。 In a normal electrolyzed water regulating device composed of an electrolysis unit and a water purification unit,
In order to separate the water flowing into the inlet of the electrolysis unit into alkaline water and acidic water, an electrode chamber provided with one + electrode plate and −electrode plate was divided into two electrode chambers by an ion separation diaphragm. A primary electrolysis unit;
Only alkaline water generated in the primary electrolysis unit is allowed to flow into three weakly alkaline waters having high concentration of active hydrogen for drinking, which are three electrolytic ionic waters, strong alkaline waters for washing, and acidic waters for face washing. Therefore, an electrode chamber in which one + electrode plate and two −electrode plates are installed is composed of a secondary electrolysis unit divided into three electrode chambers by two ion separation membranes. Water conditioner. 前記１次電解部に隔膜をさらに設置して＋電極板と−電極板との間に２つの隔膜を位置させ、この２つの隔膜の間に流出する中性水を２次電解部の流入口に流入させるように構成されたことを特徴とする請求項１記載の電気分解整水器。 A diaphragm is further installed in the primary electrolysis part, two diaphragms are positioned between the + electrode plate and the-electrode plate, and neutral water flowing between the two diaphragms is introduced into the inlet of the secondary electrolysis part. The electrolyzed water conditioner according to claim 1, wherein the water purifier is configured to flow into the water. 前記２次電解部で生成される弱アルカリ水は飲料水排出口へ排出されることを特徴とする請求項１または２記載の電気分解整水器。 The electrolyzed water regulating apparatus according to claim 1 or 2, wherein the weak alkaline water generated in the secondary electrolysis unit is discharged to a drinking water discharge port. 前記１次電解部で生成される酸性水は前記２次電解部から排出される酸性水と合流して洗顔水排出口へ排出されることを特徴とする請求項１または２記載の整水器。 3. The water conditioner according to claim 1, wherein the acidic water generated in the primary electrolysis unit merges with the acidic water discharged from the secondary electrolysis unit and is discharged to a face washing water discharge port. 4. . 前記２次電解部で生成される強アルカリ水は洗浄水排出口へ排出されることを特徴とする請求項１または２記載の電気分解整水器。 The electrolyzed water regulating device according to claim 1 or 2, wherein the strong alkaline water generated in the secondary electrolysis unit is discharged to a washing water discharge port.
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