JP3694042B2 - Electrolyzed water generator - Google Patents
Electrolyzed water generator Download PDFInfo
- Publication number
- JP3694042B2 JP3694042B2 JP13335394A JP13335394A JP3694042B2 JP 3694042 B2 JP3694042 B2 JP 3694042B2 JP 13335394 A JP13335394 A JP 13335394A JP 13335394 A JP13335394 A JP 13335394A JP 3694042 B2 JP3694042 B2 JP 3694042B2
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- Prior art keywords
- water
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- treated
- electrolyzed
- electrolytic
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Description
【0001】
【産業上の利用分野】
本発明は、水または食塩水等の原水を陽電極と陰電極間で電気分解して電解水を生成する電解水生成装置に関するものである。
【0002】
【従来の技術】
従来より、例えば内部が隔膜によって陽極室と陰極室とに仕切られていて、これらの陽極室と陰極室にそれぞれ陽電極と陰電極を互いに対向するように配設した電解槽を備えて、陽極室と陰極室に連続的に被処理水導入管より被処理水を導入し、供給された被処理水を直流電圧が印加された両電極間で電気分解して陽極室においては被処理水中に酸性イオンを含有する電解水を生成し、陰極室においては被処理水中にアルカリ性イオンを含有する電解水を生成させ、その後に電気分解された電解水を電解水導出管から導出するようにした電解水生成装置はよく知られている。
【0003】
【発明が解決しようとする課題】
ところで、上記の電解槽内には被処理水が被処理水導入管から電解水導出管に向かって一方向に流れているので、被処理水導入管付近では被処理水は殆ど電気分解されていないが、電解水導出管に向かうにつれて被処理水の電気分解が進んでその電気伝導度を増し、電解水導出管付近では電気伝導度が最大となっている。そして、両電極間のある位置における+極から−極に流れる電流密度をJとすると(他の条件を一定として)、Jは次の数2
【0004】
【数2】
J=(電圧×電気伝導度)/電極間の距離
で表される。ここで電極間の距離が一定なので、電流密度Jは電解水導出管付近になるほど大きくなる。したがって、被処理水を通して流れる電流は電解水導出管側ほど大きいため、このような電解槽においては、電解水導出管付近の電極表面のほうが被処理水導入管付近の電極表面よりも電価の移動に伴うストレスが大きくかかり、よって被処理水導入管付近の電極がそれほど劣化していなくても電解水導出管付近の電極表面が相当程度に劣化してしまって、この電解水導出管付近の電極表面の劣化によって電極自体の寿命が決定されてしまい、電極の耐久性が損なわれるという問題点を有していた。
【0005】
【発明の目的】
本発明は、上記問題点を解決するために、電極表面の劣化度合を一定にして電極の耐久性の向上を図ることを目的とする。
【0006】
【課題を解決するための手段】
本発明は、上記の目的を達成するため、直流電圧が印加される陽電極と陰電極をその内部に対向配設して電極室を形成し、前記両電極間の一方端から被処理水を連続的に導入し前記両電極間の他方端から電気分解された電解水を連続的に排出する電解槽を備えた電解水生成装置において、前記電解室の被処理水が連続的に導入される側に位置する前記電極間の間隔よりも前記電解室にて電気分解によって処理された電解水が排出される側に位置する前記電極間の間隔を大きくしたことを特徴とする電解水生成装置直流電圧が印加される陽電極と陰電極をその内部に対向配設して電極室を形成し、前記両電極間の一方端から被処理水を連続的に導入し前記両電極間の他方端から電気分解された電解水を連続的に排出する電解槽を備えた電解水生成装置において、前記電解室の被処理水が連続的に導入される側に位置する前記電極間の間隔よりも前記電解室にて電気分解によって処理された電解水が排出される側に位置する前記電極間の間隔を大きくしたことを特徴とする電解水生成装置を提供するものである。
【0007】
本発明の実施にあたっては、被処理水導入管が連結された方の両電極間の間隔をa及びその両電極間の電気伝導度をσinとし、一方前記電解水導出管が連結された方の両電極間の間隔をb及びその両電極間の電気伝導度をσout とした場合、次の数3の関係式、即ち、
【数3】
(b/a)≒(σ out /σ in )
を満たすようにすることが望ましい。
【0009】
【発明の作用・効果】
上記のように構成した本発明の電解水生成装置においては、両電極間を流れる処理水の電気伝導度に勾配があっても、両電極が、被処理水導入管が連結された方の電極間の間隔よりも前記電解水導出管が連結された方の電極間の間隔が大きくなるように配設されているため、上記数2の関係式に従うと、被処理水導入管付近と電解水導出管付近との電流密度Jの差は、電極間の間隔が一定の場合の電流密度Jの差よりも小さくなる。したがって、本発明によれば、被処理水導入管付近の電極表面と電解水導出管付近の電極表面の劣化度合の差は小さくなり、その結果電極の耐久性の向上を図ることができる。
【0010】
そしてこの際の両電極を、上記の数3:(b/a)≒(σout/σin)の関係(aは被処理水導入管が連結された方の両電極間の間隔、bは電解水導出管が連結された方の両電極間の間隔、σinは被処理水導入管が連結された方の両電極間の電気伝導度、σout は電解水導出管が連結された方の両電極間の電気伝導度)を満たすように配設すれば、被処理水導入管付近と電解水導出管付近との電流密度Jの差はほとんどなくなり、すなわち被処理水導入管付近の電極表面と電解水導出管付近の電極表面の劣化度合に有意の差がなくなるため、電極の耐久性を向上させるという効果は更に高まる。
【0011】
【実施例】
以下、本発明を図面を用いて説明する。
図1には本発明の電解水生成装置の一実施例が示されている。この電解水生成装置は、電解槽本体11の内部が隔膜12によって陽極室13と陰極室14とに仕切られていて、この陽極室13と陰極室14にそれぞれ陽電極15と陰電極16とが互いに対向するように配設された電解槽10を備えている。この両電極15,16は直流電源(図示しない。)に接続されていて、両電極室13,14に供給された処理水を両電極15,16間にて電気分解し、それぞれ酸性水とアルカリ性水を生成するように構成されている。
【0012】
この電解槽10の陽極室13及び陰極室14の一方の端部には、電気分解を行うための被処理水(塩濃度0.05〜0.14%の希塩水)を被処理水供給源(図示しない。)からポンプなどを用いて導入する経路である被処理水導入管20が、導入管20a及び導入管20bに分岐して連結されている。また、陽極室13のもう一方の端部には電気分解によって生成した酸性水を導出する酸性水導出管21が、同様に陰極室14のもう一方の端部には電気分解によって生成したアルカリ性水を導出するアルカリ性水導出管22が連結されている。
【0013】
この実施例の電解水生成装置における陽電極15及び陰電極16は、上記の数3:(b/a)≒(σout/σin)の関係(aは被処理水導入管20a,20bが連結された方の両電極15,16間の間隔、bは電解水導出管21,22が連結された方の両電極15,16間の間隔、σinは被処理水導入管20a,20bが連結された方の両電極15,16間の電気伝導度、σout は電解水導出管21,22が連結された方の両電極15,16間の電気伝導度)を満たすように配設されている。
【0014】
このように構成された電解水生成装置を用いて被処理水を供給しつつ両電極15,16間で電気分解を行って電解水を生成させる際には、両電解室13,14内の被処理水は、被処理水導入管20a,20b付近では殆ど電気分解されていないが、酸性水導出管21及びアルカリ性水導出管22に向かうにつれて被処理水の電気分解が進んでその電気伝導度を増し、酸性水導出管21及びアルカリ性水導出管22付近では電気伝導度が最大となっている。しかしながら上述のとおり陽電極15及び陰電極16は、上記の数3:(b/a)≒(σout/σin)の関係を満たすように配設されているので、上記の数2の関係式より明らかなように、被処理水導入管20a,20b付近と電解水導出管21,22付近との電流密度Jの差はほとんどなく、すなわち被処理水導入管20a,20b付近の電極15,16表面と電解水導出管21,22付近の電極15,16表面の劣化度合に有意の差は生じない。したがって、電極の耐久性を向上を図ることができる。
【0015】
なお上記実施例においては、電解槽として電解槽本体11内部を隔膜12によって陽極室13及び陰極室14に区画したタイプの電解槽10を用いたが、隔膜がなく、電解槽本体内部の電極室が一室のタイプの電解槽を用いてもよい。このようなタイプの電解槽を用いた場合では、一本の処理水導入管と一本の電解水排出管を備えた電解水生成装置として構成される。
【図面の簡単な説明】
【図1】 本発明の一実施例にかかる電解水生成装置を示す概略図である。
【符号の説明】
10…電解槽、12…隔膜、13…陽極室、14…陰極室、15…陽電極、16…陰電極、20,20a,20b…被処理水導入管、21…酸性水導出管、22…アルカリ性水導出管。[0001]
[Industrial application fields]
The present invention raw water, such as water or saline relates electrolytic water generation apparatus for generating electrolysis to the electrolytic water between the anode and the cathode.
[0002]
[Prior art]
Conventionally, for example, inside it has been partitioned into an anode chamber and a cathode chamber by a diaphragm, each of these anode chamber and the cathode chamber includes an arranged underneath electrolytic tank so as to face each other with positive electrode and negative electrode, continuously introducing treatment water from the treated water inlet pipe explicitly electrode chamber and the cathode chamber, the in electrical degradation to the anode chamber to be treated water supplied between the electrodes to which a DC voltage is applied process to generate electrolytic water containing an acidic ion in water, in the negative electrode chamber to produce electrolytic water containing alkaline ions in the water to be treated, to derive the subsequently electrolyzed electrolytic water from the electrolytic water discharge pipe Such an electrolyzed water generating apparatus is well known.
[0003]
[Problems to be solved by the invention]
Where, in the above electrolytic cell so treated water is flowing in one direction toward the electrolytic water outlet pipe from the treatment water inlet pipe, in the vicinity of the treatment water inlet pipe water to be treated is almost electrolyzed not but increasing its electrical conductivity progressed electrolysis of the for-treatment water toward the electrolytic water guide extraction tube, the electric conductivity in the vicinity of electrolytic water guide extraction pipe is maximum. When the current density flowing from the positive electrode to the negative electrode at a certain position between the two electrodes is J (other conditions are constant), J is expressed by the following equation 2
[0004]
[Expression 2]
J = (voltage × electrical conductivity) / distance between electrodes. Here, since the distance between the electrodes is constant, the current density J increases as to approximately the electrolytic water guide extraction tube. Therefore, since the current flowing through the treated water is large enough electrolyzed water guide extraction tube side, in such electrolytic cells, electrodeposition than the electrode surface of the vicinity of the treated water inlet pipe towards the electrode surface in the vicinity of the electrolytic water guide extraction tube it takes a large stress due to the movement of the valence, therefore it got deteriorated considerable degree the electrode surface in the vicinity of the electrolytic water guide extraction tube even when no electrodes in the vicinity of the treatment water inlet pipe so much deteriorated, the electrolytic water guide The life of the electrode itself is determined by the deterioration of the electrode surface near the outlet tube, and the durability of the electrode is impaired.
[0005]
OBJECT OF THE INVENTION
The present invention, in order to solve the above SL problems, and an object thereof is to improve the durability of the to electrodes the degree of deterioration of the electrode surface constant.
[0006]
[Means for Solving the Problems]
In order to achieve the above object, the present invention forms an electrode chamber by arranging a positive electrode and a negative electrode, to which a DC voltage is applied, facing each other, and forms water to be treated from one end between the two electrodes. In an electrolyzed water generating apparatus having an electrolyzer that continuously introduces and electrolyzes electrolyzed electrolyzed water from the other end between the electrodes, water to be treated in the electrolysis chamber is continuously introduced. electrolytic water generation apparatus a DC being characterized in that to increase the distance between the electrodes electrolytic water treated by electrolysis in the electrolysis chamber than the spacing between the electrodes located on the side is located on the side to be discharged A positive electrode and a negative electrode to which a voltage is applied are arranged opposite to each other to form an electrode chamber, and water to be treated is continuously introduced from one end between the two electrodes and from the other end between the two electrodes. electrolytic aquatic including the electrolytic tank for continuously discharging the electrolyzed electrolytic water In the apparatus, the said electrolysis chamber electrolytic water treatment water is treated by electrolysis in the electrolysis chamber than the spacing between the electrodes located on the side which is introduced continuously in is located on the side to be discharged It is an object of the present invention to provide an electrolyzed water generating device characterized in that an interval between electrodes is increased.
[0007]
The practice of the present invention, the distance between the electrodes of the person who is treated water inlet pipe connected to the σin electrical conductivity between a and two electrodes, whereas the direction which electrolytic water guide extraction pipe is connected Where b is the distance between the two electrodes and σout is the electric conductivity between the two electrodes,
[Equation 3]
(B / a) ≈ (σ out / σ in )
It is desirable to satisfy.
[0009]
[Operation and effect of the invention]
Oite the electrolytic water generation apparatus of the present invention constructed as above SL, even if there is a gradient in the electrical conductivity of the treated water flowing between both electrodes, both electrodes, the water to be treated inlet pipe connected the interval between the square of the inter-electrode of the person who electrolytic water guide extraction pipe is connected than the distance between the electrodes is arranged to be larger, according to the number 2 relationship, the treatment water inlet pipe difference in current density J in the vicinity of and around the electrolytic water guide decane, spacing between electrodes is less than the difference between the current density J in the case of a constant. Therefore, according to the present invention, the difference in degree of degradation of the electrode surface in the vicinity of the electrolytic water guide extraction pipe water to be treated inlet pipe near the electrode surface is reduced, it is possible to improve the durability of the resulting electrode.
[0010]
Then the two electrodes at this time, the number of the 3: (b / a) ≒ (σout / σin) relationship (a spacing between the electrodes towards the treated water inlet pipe is connected, b electrolytic water spacing between the electrodes towards the electrically extraction pipe is connected, Shigumain the electric conductivity between the electrodes towards which the treated water inlet pipe is connected, Shigumaout both those who electrolytic water guide extraction pipe is connected if arranged so as to satisfy the electrical conductivity) between the electrodes, the difference between the current density J of the vicinity of the electrolytic water guide extraction pipe and the vicinity of the treated water inlet pipe almost no, i.e. the electrode surface in the vicinity of the treated water inlet pipe and the difference between the significant degree of degradation of the electrode surface in the vicinity of the electrolytic water guide extraction pipe is eliminated, the effect of improving the durability of the electrode further increases.
[0011]
【Example】
Hereinafter, the present invention will be described with reference to the drawings.
FIG. 1 shows an embodiment of the electrolyzed water generating apparatus of the present invention. In this electrolyzed water generator, the inside of the electrolytic cell body 11 is partitioned into an
[0012]
At one end of the
[0013]
[0014]
In forming the electrolytic water by performing electrolysis between the two
[0015]
In the above embodiment, the electrolytic cell 10 of the type in which the inside of the electrolytic cell main body 11 is divided into the
[Brief description of the drawings]
FIG. 1 is a schematic view showing an electrolyzed water generating apparatus according to an embodiment of the present invention.
[Explanation of symbols]
10 ... the electrolytic cell, 12 ... diaphragm, 13 ... anode chamber, 14 ... cathode chamber, 15 ... positive electrode, 16 ... cathode, 20, 20a, 20b ... treatment water inlet pipe, 21 ... acidic water outlet pipe, 22 ... Alkaline water outlet tube.
Claims (3)
前記電解室の被処理水が連続的に導入される側に位置する前記電極間の間隔よりも前記電解室にて電気分解によって処理された電解水が排出される側に位置する前記電極間の間隔を大きくしたことを特徴とする電解水生成装置。A positive electrode and a negative electrode to which a DC voltage is applied are arranged oppositely to form an electrode chamber, and water to be treated is continuously introduced from one end between the two electrodes, and the other end between the two electrodes. In the electrolyzed water generating apparatus provided with an electrolyzer that continuously discharges electrolyzed electrolyzed water from
Between the electrodes of the electrolyte chamber electrolytic water treatment water is treated by electrolysis in the electrolysis chamber than the spacing between the electrodes located on the side which is introduced continuously in is located on the side to be discharged An electrolyzed water generating device characterized in that the interval is increased.
前記両電解室の被処理水が連続的に導入される側に位置する前記電極間の間隔よりも前記両電解室にて電気分解によって処理された電解水が排出される側に位置する前記電極間の間隔を大きくしたことを特徴とする電解水生成装置。A positive electrode and a negative electrode, to which a DC voltage is applied, are arranged opposite to each other through a diaphragm to form a cathode chamber as an anode chamber, and water to be treated is continuously introduced from one end between the electrodes. In the electrolyzed water generating device comprising an electrolyzer that continuously discharges electrolyzed electrolyzed water from the other end between the electrodes ,
The electrode located on the side where the two electrolysis chambers electrolytic water treatment water is treated by electrolysis in the two electrolysis chambers than the spacing between the electrodes located on the side which is introduced continuously in is discharged The electrolyzed water generating apparatus characterized by increasing the interval between them.
【数1】
(b/a)≒ (σout /σin)The distance between the electrodes located on the side where the treated water is continuously introduced is a, and the electrical conductivity between the electrodes is σin, while the both electrodes located on the side where the electrolyzed water is derived 3. The electrolyzed water generating device according to claim 1, wherein the following equation 1 is satisfied, where b is an interval between them and σout is an electric conductivity between the electrodes.
[Expression 1]
(B / a) ≒ (σout / σin)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13335394A JP3694042B2 (en) | 1994-06-15 | 1994-06-15 | Electrolyzed water generator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13335394A JP3694042B2 (en) | 1994-06-15 | 1994-06-15 | Electrolyzed water generator |
Publications (2)
Publication Number | Publication Date |
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JPH07328630A JPH07328630A (en) | 1995-12-19 |
JP3694042B2 true JP3694042B2 (en) | 2005-09-14 |
Family
ID=15102740
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JP13335394A Expired - Fee Related JP3694042B2 (en) | 1994-06-15 | 1994-06-15 | Electrolyzed water generator |
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JP2012240037A (en) * | 2011-05-24 | 2012-12-10 | Panasonic Corp | Electrolytic cell and electrolyzed water producing apparatus |
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1994
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JPH07328630A (en) | 1995-12-19 |
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