JP2006026578A - Electrolytic water producing method and electrolytic water producing apparatus - Google Patents

Electrolytic water producing method and electrolytic water producing apparatus Download PDF

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JP2006026578A
JP2006026578A JP2004211486A JP2004211486A JP2006026578A JP 2006026578 A JP2006026578 A JP 2006026578A JP 2004211486 A JP2004211486 A JP 2004211486A JP 2004211486 A JP2004211486 A JP 2004211486A JP 2006026578 A JP2006026578 A JP 2006026578A
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JP4512842B2 (en
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Hiroyuki Yoshida
浩之 吉田
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Abstract

<P>PROBLEM TO BE SOLVED: To improve electrolysis efficiency and to adjust pH between 5.8 and 8.6 by making gaseous hydrogen and gaseous oxygen intermingle in treated water (electrolytic water) by performing electrolysis without via a diaphragm in a water path and further narrowing distance between an electrode and an inside wall of an electrolytic cell. <P>SOLUTION: The subject electrolytic water producing apparatus is provided with an electrolytic current controlling section comprising an electrolytic cell(d) at an upper side wall of which a water inlet port (j) and a water ejecting port (q) are oppositely equipped, positive and negative electrodes (a; b; c) composed of a plurality of planar electrodes (a; b; c) which are flatly arranged in a longitudinal direction of the electrolytic cell (d) and are arranged to face each other at intervals in a transverse direction, and a polarity inversion circuit for electrolyzing water to be treated while periodically or intermittently inverting applied polarity to the positive and negative electrodes (a; b; c). By electrolyzing water to be treated while making the water flow in one direction via between the positive and negative electrodes (a; b; c), the electrolytic water in a state where gaseous hydrogen and gaseous oxygen intermingle with each other is produced. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

この発明は、水道水その他の被処理水を多電極型電解槽に導入し水質改善をおこなう電解水生成方法及び電解水生成装置に関する。   The present invention relates to an electrolyzed water generating method and an electrolyzed water generating apparatus for introducing tap water and other treated water into a multi-electrode electrolytic cell to improve water quality.

従来、水道水などの水質を改善する器具として、活性炭でろ過させる方式や電気分解によって水分子を分解させる方法などが知られている。最近では、磁石を利用して、磁力線を作用させて水質の改善を図る器具が実用化されている。しかし、これらの器具機械は、長期の使用が難しくまた、磁力線についても、磁石の強さを示す「ガウス」の低いものや、リング状の内側を使用するものは、減磁作用があり、水質改善の効果に欠ける問題があった。   Conventionally, as a device for improving water quality such as tap water, a method of filtering with activated carbon or a method of decomposing water molecules by electrolysis is known. Recently, an instrument that uses a magnet to improve the water quality by applying magnetic force lines has been put into practical use. However, these appliances are difficult to use for a long period of time, and the magnetic field lines that have a low "Gauss" that indicates the strength of the magnet and those that use a ring-shaped inside have a demagnetizing action, There was a problem of lack of improvement effect.

今日、電解水生成装置と称する製品が市場提供されているが、そのほとんどは、陰陽電極間に隔膜を介した電気分解方式であり、アルカリ性と酸性に分解して吐水させる方法であった(例えば、特許文献1を参照。)。
特開平6−312186号公報
Today, products called electrolyzed water generators are available on the market, most of which are electrolysis systems with a diaphragm between the yin and yang electrodes, which decomposes alkaline and acidic water and discharges water (for example, , See Patent Document 1).
JP-A-6-312186

しかしながら、原水のpHを変えるということは医療効果を生む反面、薬事法の管理の下に飲用しなくてはならず、不特定多数の消費者の消費者すべてが飲用出来ないという問題がある。   However, changing the pH of the raw water produces a medical effect, but it must be drunk under the control of the Pharmaceutical Affairs Law, and there is a problem that all consumers of an unspecified number of consumers cannot drink.

また、この種のものでは、電気分解により発生する水素ガスと酸素ガスが分別されて吐水されてしまい、単一の水素ガスの多い水しか飲用できなかった。   Also, with this type, hydrogen gas and oxygen gas generated by electrolysis are separated and discharged, and only a single hydrogen gas-rich water can be drunk.

さらに、酸素ガスの多い水を飲用しようとすると、酸性の水を飲用するしかなく、人体に良いとはいえない。   Furthermore, if you try to drink water with a lot of oxygen gas, you can only drink acidic water, which is not good for the human body.

人体体液は、弱アルカリ性(pH7.35)であるが、人体体液に近く、水素ガス及び酸素ガスの含有量の多い水を生成する装置は無い。水質基準でもpH5.8〜8.6と飲用適合のpHは中性に近い。   Human body fluid is weakly alkaline (pH 7.35), but there is no device that produces water with a high content of hydrogen gas and oxygen gas that is close to human body fluid. Even on a water quality basis, the pH of 5.8 to 8.6 and the pH suitable for drinking are close to neutrality.

さらに、従来被処理水を電気分解する方法では、陰陽の電極間の幅だけを注視しており、電極と電解槽の内壁との間隔については、無視されていた。   Furthermore, in the conventional method of electrolyzing water to be treated, only the width between the yin and yang electrodes is watched, and the distance between the electrodes and the inner wall of the electrolytic cell has been ignored.

しかし、被処理水が電極間を通過するため、電極間の幅を狭めることで、電解効率がよくなるが、被処理水を通過させなくてはならないため、その幅を狭めるには限度があった。また、電解効率が上がり、水素ガスと酸素ガスの発生が増大すると、無隔膜電解の場合、酸素ガスの発生に影響されpHがアルカリ側にシフトし、中性域の電解水を取り出すことが難しかった。   However, since the water to be treated passes between the electrodes, reducing the width between the electrodes improves the electrolysis efficiency. However, since the water to be treated must be passed, there is a limit to reducing the width. . In addition, when the electrolysis efficiency increases and the generation of hydrogen gas and oxygen gas increases, in the case of diaphragmless electrolysis, the pH shifts to the alkali side due to the generation of oxygen gas, and it is difficult to extract neutral electrolyzed water. It was.

そこで、水道水その他の被処理水を電気分解において、隔膜を介さず陰陽の電気分解を行い、さらに分解して二種類の水に分けるのではなく、一種類の水を吐水させ、水素ガスと酸素ガスが混在した電解水を吐水することが要請される。   Therefore, in electrolysis of tap water and other treated water, electrolysis of yin and yang is not carried out without a diaphragm, and it is not further decomposed and divided into two types of water, but one type of water is discharged, hydrogen gas and It is required to discharge the electrolyzed water mixed with oxygen gas.

また、電気分解の効率を高めるためには、電解質を含む溶液の濃度を上げたり、電極癇の距離を狭めることしかしていなかった。そこで、電極間の幅だけを注視するのではなく、電極と電解槽の内壁との間の距離を検討する必要がある。   Moreover, in order to increase the efficiency of electrolysis, the concentration of the solution containing the electrolyte has only been increased or the distance between the electrode cages has been reduced. Therefore, it is necessary to consider the distance between the electrode and the inner wall of the electrolytic cell, not just the width between the electrodes.

本発明は、このような事情に鑑みなされたものであって、上記課題を解消し、水道水その他の被処理水を多電極型電解槽に導入し、無隔膜で電解水を生成し、さらに、電極と電解槽の内壁との間隔を狭くすることによって水質改善を行う電解水生成方法及び電解水生成装置を提供するものである。   The present invention has been made in view of such circumstances, solves the above problems, introduces tap water and other treated water into a multi-electrode electrolytic cell, generates electrolyzed water with a diaphragm, and The present invention provides an electrolyzed water generating method and an electrolyzed water generating apparatus for improving water quality by narrowing the distance between an electrode and an inner wall of an electrolytic cell.

課題を解決するために本発明は、水道水その他の被処理水を多電極型電解槽に導入し水質改善をおこなう電解水生成方法の改善であって、
槽内に複数の板状又は円筒状の電極を離隔して並設し、隣接する電極間で陰陽電極を構成するとともに、上部槽端の側壁に入水口と吐水口を対向して設け、前記陰陽電極間を経由して被処理水を一方向に流通させ、かつ、該陰陽電極への印加極性を周期的又は間欠的に反転させながら被処理水の電気分解をおこなうことにより、水素ガス及び酸素ガスが混在した状態の電解水を生成するようにしたことを特徴とするものである。
In order to solve the problem, the present invention is an improvement of a method for generating electrolyzed water in which tap water or other treated water is introduced into a multi-electrode electrolytic cell to improve water quality,
A plurality of plate-like or cylindrical electrodes are arranged in parallel in the tank, and a negative and positive electrode is formed between adjacent electrodes, and a water inlet and a water outlet are provided opposite to the side wall of the upper tank end, By flowing the water to be treated in one direction via the yin and yang electrodes and performing electrolysis of the water to be treated while periodically or intermittently reversing the polarity applied to the yin and yang electrodes, hydrogen gas and Electrolytic water in a state where oxygen gas is mixed is generated.

また、上記方法を実施するための電解水生成装置であって、
上部側壁に入水口と吐水口を対設した電解槽と、
該電解槽の縦断方向に平面配置され、かつ、横断方向に離隔して対向設置された板状電極から構成され、それぞれの電極の上下端のいずれかに水路をつなぐクリアランスを設け、かつ、設置内外方向に該クリアランスを上下に交互配置した陰陽電極と、
該陰陽電極への印加極性を周期的又は間欠的に反転させながら被処理水の電気分解をおこなうための極性反転回路を含む電解電流制御部を具備し、
前記陰陽電極間を水路として被処理水を一方向に流通させ、電解生成した水素ガス及び酸素ガスが混在した状態の電解水を取り出すようにしたことを特徴とするものである。
An electrolyzed water generating apparatus for carrying out the above method,
An electrolytic cell having a water inlet and a water outlet on the upper side wall;
It is composed of plate-like electrodes that are arranged in a plane in the longitudinal direction of the electrolytic cell and are opposed to each other in the transverse direction, and a clearance that connects a water channel is provided at either the upper or lower end of each electrode. A yin and yang electrode in which the clearance is alternately arranged up and down in the inner and outer directions;
An electrolytic current control unit including a polarity reversing circuit for performing electrolysis of water to be treated while periodically or intermittently reversing the polarity applied to the yin and yang electrodes;
The water to be treated is circulated in one direction by using a water channel between the yin and yang electrodes, and electrolyzed water in a state in which hydrogen gas and oxygen gas generated by electrolysis are mixed is taken out.

ここで、電極間には隔膜を設けないこと(無隔膜電解をおこなうこと)、及び槽内壁と最外設置電極との間隔を5mm以内に狭めることが重要である。   Here, it is important not to provide a diaphragm between the electrodes (perform non-diaphragm electrolysis) and to narrow the distance between the inner wall of the tank and the outermost electrode within 5 mm.

本発明によれば、被処理水の電解生成を一時中断させること無く、電解水を吐水することができる。   According to the present invention, the electrolyzed water can be discharged without temporarily interrupting the electrolysis of the water to be treated.

また、周期的・間欠的に反転させながら被処理水の電気分解を行う場合においては、使用時間や頻度に関係なく、同等に洗浄と電解水が生成されて、尚且つ、電極板へのカルシウムやマグネシウムの付着や水素と酸素の気泡の付着を防止できる。   In addition, when electrolyzing the water to be treated while being inverted periodically and intermittently, cleaning and electrolyzed water are equally generated regardless of the usage time and frequency, and the calcium to the electrode plate And adhesion of magnesium and bubbles of hydrogen and oxygen can be prevented.

さらに、電解槽内に挿入されている電極と電解槽の内壁との間の隙間を狭めていくことで、電気分解の効率を高めることが出来るため、水素ガス及び酸素ガスの発生を促進することが出来る。しかも、電解水のpHを5.8〜8.6範囲に調整できる。   Furthermore, since the efficiency of electrolysis can be increased by narrowing the gap between the electrode inserted in the electrolytic cell and the inner wall of the electrolytic cell, the generation of hydrogen gas and oxygen gas is promoted. I can do it. Moreover, the pH of the electrolyzed water can be adjusted in the range of 5.8 to 8.6.

本発明を実施するための最良の形態は、上記構成において、陰陽電極間に隔膜などの分離壁を設けず、電解中に水素ガスと酸素ガスを混在させて単一水を吐水させるものであり、隔膜がないため、電極間の被処理水中では自由にプラスイオンとマイナスイオンが混合され、電解生成した水素ガス及び酸素ガスが混在した状態の電解水を単一水路より吐水させるようにしている。   In the above configuration, the best mode for carrying out the present invention is that a separation wall such as a diaphragm is not provided between the yin and yang electrodes, and hydrogen gas and oxygen gas are mixed during electrolysis to discharge single water. Since there is no diaphragm, positive ions and negative ions are freely mixed in the water to be treated between the electrodes, and electrolyzed water in a state where the hydrogen gas and oxygen gas generated by electrolysis are mixed is discharged from a single water channel. .

ここで、槽内の最外設置電極と、槽内壁との間の距離は、5mm以内にすることが望まれる。電気分解の効率を高めるためである。これにより、電解水のpHを5.8〜8.6範囲に調整できる。ただし、最外設置電極と電解槽の内側は完全に接触せず、少なくとも、電極が被処理水で濡れた状態になるようにしなければならない。   Here, it is desirable that the distance between the outermost installed electrode in the tank and the inner wall of the tank be within 5 mm. This is to increase the efficiency of electrolysis. Thereby, pH of electrolysis water can be adjusted to 5.8-8.6 range. However, the outermost electrode and the inside of the electrolytic cell are not completely in contact with each other, and at least the electrode must be in a wet state with the water to be treated.

さらに、電極間の幅はそれぞれの電極(以下、電極板。)が交互に接触しないように、電解槽の上下端に電極板をささえる電極板固定ガイドを設けて、すべての電極板間の幅を一定に保つのが好ましい。また、それぞれの電極の上下端のいずれかに水路をつなぐクリアランスを設け、かつ、設置内外方向に該クリアランスを上下に交互配置して一方向水路を形成している。   Furthermore, the width between the electrodes is such that electrode plates fixing guides for holding the electrode plates are provided at the upper and lower ends of the electrolytic cell so that the electrodes (hereinafter referred to as electrode plates) do not contact each other alternately. Is preferably kept constant. In addition, a clearance for connecting the water channel is provided at either the upper or lower end of each electrode, and the clearance is alternately arranged in the vertical direction inside and outside the installation to form a one-way water channel.

なお、電極材料は、チタン、フェライト、ステンレスその他の非磁性金属、又はこれらに白金を被覆したものから選択されるのが好ましい。   The electrode material is preferably selected from titanium, ferrite, stainless steel and other nonmagnetic metals, or those coated with platinum.

そして、電解槽(d)上端の片方(j)から槽内へ導入された被処理水は、電極板(b)と電極板固定ガイド(e)の隙間(a-1)を通り電極間を水路として槽内を一方向に移動する。このとき、電極板(a)と電極板(c)へはプラスの電流電圧が印加されており、電極板(b)にはマイナスの電流電圧が印加されている。   And the to-be-processed water introduce | transduced in the tank from one side (j) of an electrolytic cell (d) upper end passes through the clearance gap (a-1) of an electrode plate (b) and an electrode plate fixed guide (e), and between electrodes. It moves in one direction as a waterway in the tank. At this time, a positive current voltage is applied to the electrode plate (a) and the electrode plate (c), and a negative current voltage is applied to the electrode plate (b).

また、それぞれの電極板(a)(b)(c)には少なくとも直流電圧10vと電流0.2Aが交差しており、電極間を通過する水はこの直流電圧・電流の印加を受けることになる。さらに、一定時間を経過すると、電解電流制御部(r)により印加極性を反転させ、これを繰り返すものである〔所謂、交流電解。〕   Each electrode plate (a), (b), and (c) has at least a DC voltage of 10v and a current of 0.2A intersecting, and the water passing between the electrodes is subjected to the application of the DC voltage / current. Become. Furthermore, when a certain time has elapsed, the applied current control unit (r) reverses the applied polarity and repeats this [so-called AC electrolysis. ]

ところで、電極(a)と(c)に隣接している電解槽の内側(d-1)には、狭い水路があるが、この距離(水路幅)は多くとも5mm以下と狭くすることで、電解電流が効率よく電極(a)(b)(c)に流れるようにしている。この距離は狭いほど電解効率がよくなり、電極(a)と(b)が電解槽の内壁(d-1)に接触しない程度の隙間は必要となる。   By the way, the inner side (d-1) of the electrolytic cell adjacent to the electrodes (a) and (c) has a narrow water channel, but this distance (water channel width) is at most 5 mm or less, The electrolytic current is made to efficiently flow to the electrodes (a), (b) and (c). The narrower the distance, the better the electrolysis efficiency, and a gap is required so that the electrodes (a) and (b) do not contact the inner wall (d-1) of the electrolytic cell.

本発明の一実施例を添付図面を参照して以下説明する。   An embodiment of the present invention will be described below with reference to the accompanying drawings.

図1は、本発明方法を実施するための電解水生成装置の縦断面視構成概要図である。   FIG. 1 is a vertical cross-sectional structural schematic diagram of an electrolyzed water generating apparatus for carrying out the method of the present invention.

図2は、同じく電解水生成装置の横断面視構成概要図である。   FIG. 2 is a schematic cross-sectional view of the electrolyzed water generator.

図3は、同じく電極板の構成概要図である。   FIG. 3 is a schematic configuration diagram of the electrode plate.

図4は、同じく電解電流制御系統を説明するブロック図である。   FIG. 4 is a block diagram illustrating the electrolytic current control system.

図示するように、電解槽(d)の上下端(h)(i)には、電極板(a)(b)(c)装着のための電極板固定ガイド(e)が設けられている。そのガイド(e)に電極板(a)(b)(c)が装着される。ここで、それぞれの電極板(a)(b)(c)上下端のいずれかと電極板固定ガイド(e)との間に隙間〔クリアランス(a-1) (b-1) (c-1) 〕を設け、一方向水路(k〜p)を形成している。   As shown in the drawing, electrode plate fixing guides (e) for mounting the electrode plates (a), (b), and (c) are provided at the upper and lower ends (h) and (i) of the electrolytic cell (d). Electrode plates (a), (b), and (c) are attached to the guide (e). Here, a gap [clearance (a-1) (b-1) (c-1) between any one of the upper and lower ends of each electrode plate (a) (b) (c) and the electrode plate fixing guide (e). ] To form a one-way water channel (k to p).

電極板(a)(b)(c)の側面には、接続端子(f-1)(f-2)(f-3)が設けられており、電解電流制御部(r)に接続される。   Connection terminals (f-1), (f-2), and (f-3) are provided on the side surfaces of the electrode plates (a), (b), and (c) and are connected to the electrolytic current control unit (r). .

電解電流制御部(r)では、(s)の電源部より、直流電圧が少なくとも10V電流0.2Aが電解電流制御部(r)に供給されており、流量センサー(t)が水が流れると所定のパルスをマイコン部(U)で感知させる。マイコン部(U)では、(f-1)(f-2)(f-3)へ供給する所定の電解電流値、電圧を記憶させ指示するほか、電源LED(X)及び生成状態LED(Y)の点灯を指示する。   In the electrolysis current control unit (r), when the DC voltage is at least 10V 0.2 A is supplied from the power source unit (s) to the electrolysis current control unit (r), and the flow rate sensor (t) flows water. A predetermined pulse is detected by the microcomputer unit (U). In the microcomputer unit (U), a predetermined electrolytic current value and voltage supplied to (f-1), (f-2), and (f-3) are stored and instructed, and a power LED (X) and a generation state LED (Y ) Is lit.

また、マイコン部(U)でプログラミングさせた所定の電解電流・電圧を(f-1)(f-2)(f-3)へ供給するが、(v)及び(w)のスイッチングにて動作反転を指示する。   In addition, a predetermined electrolytic current / voltage programmed in the microcomputer unit (U) is supplied to (f-1), (f-2), and (f-3), but operates by switching of (v) and (w). Instruct to reverse.

そこで、まず原水はIN側(j)から注水され、(l)方向及び(k)方向に通水されて、電極板(a)と電極板固定ガイド(e)とのあいだ(a-1)を通過する。   Therefore, the raw water is first poured from the IN side (j), passed in the (l) direction and (k) direction, and between the electrode plate (a) and the electrode plate fixing guide (e) (a-1) Pass through.

そして、通過した水は(m)方向へ進み、電極板(b)と電解槽ガイド(e)(b-1)とのあいだ(b-1)を通過する。通過した水は(n)方向に進み、電極板(c)と電解槽ガイド(c-1)との間を通過して、OUT側の吐水口(q)へと吐水する。   Then, the water that has passed passes in the (m) direction, and passes through (b-1) between the electrode plate (b) and the electrolytic cell guides (e) and (b-1). The passed water proceeds in the (n) direction, passes between the electrode plate (c) and the electrolytic cell guide (c-1), and discharges water to the OUT side water discharge port (q).

ここで、電極板(a)と電極板(c)にはプラス極の電流0.2〜10A、電圧5〜36vが印加されており、電極板(b)には0.2〜10A、電圧5〜36v、が印加されている。印加極性は、一定時間ごとに反転させるようにしている。   Here, positive electrode current 0.2 to 10 A and voltage 5 to 36 v are applied to the electrode plate (a) and the electrode plate (c), and 0.2 to 10 A and voltage are applied to the electrode plate (b). 5 to 36v is applied. The applied polarity is reversed every predetermined time.

IN側(j)から入水され、(a-1)を通過した水は、電極板(a)と(b)に印加された電圧電流により、水の電気分解が起こり、水素ガスと酸素ガスを発生させる。   Water that has entered from the IN side (j) and passed through (a-1) undergoes electrolysis of water due to the voltage and current applied to the electrode plates (a) and (b), and generates hydrogen gas and oxygen gas. generate.

そして、(b-1)を通過した水は、さらに電極板(b)と(c)に印加された電圧電流により、水の電気分解が起こり、水素ガスと酸素ガスが発生する。   The water that has passed through (b-1) is further electrolyzed by the voltage and current applied to the electrode plates (b) and (c) to generate hydrogen gas and oxygen gas.

そのとき、電極板(a)(c)と電解槽の内壁(d-1)には狭い水路を形成しており、電極板(a)(c)の側面を濡れた状態に保っている。ここで、水路幅の狭さは重要であり、多くとも5mm以下で、尚且つ接触しない状態に保つ必要がある。   At that time, narrow water channels are formed in the electrode plates (a) and (c) and the inner wall (d-1) of the electrolytic cell, and the side surfaces of the electrode plates (a) and (c) are kept wet. Here, the narrowness of the water channel width is important, and it is necessary to keep it at most 5 mm or less and not in contact.

その後、OUT側の吐水口(q)から取り出された電解水は、pH5.8〜8.6で水素ガスと酸素ガスを含み、酸化還元電位が低く、水の分子集団の小さな健康飲料水へ水質改善されたものとなっている。   Thereafter, the electrolyzed water taken out from the outlet (q) on the OUT side contains hydrogen gas and oxygen gas at pH 5.8 to 8.6, has a low oxidation-reduction potential, and has a small water molecular group. The water quality has been improved.

電解水生成装置の縦断面視構成概略図である。It is a longitudinal section view schematic diagram of an electrolyzed water generating device. 電解水生成装置の横断面視構成概略図である。It is a cross section view schematic diagram of an electrolyzed water generating device. 電極板の構成概略図である。It is a structure schematic diagram of an electrode plate. 電解電流制御系統を説明するブロック図である。It is a block diagram explaining an electrolysis current control system.

符号の説明Explanation of symbols

(a) 板状電極(電極板)
(b) 板状電極(電極板)
(c) 板状電極(電極板)
(d) 電解槽
(d-1) 電解槽の内壁(槽内壁)
(e) 電極板固定ガイド
(f) 接続端子
(f-1) 接続端子A
(f-2) 接続端子B
(f-3) 接続端子C
(a-1) 電極板(a)と電極板固定ガイド(e)とのクリアランス
(b-1) 電極板(b)と電極板固定ガイド(e)とのクリアランス
(c-1) 電極板(c)と電極板固定ガイド(e)とのクリアランス
(h) 上端
(i) 下端
(j) 入水口IN側
(k) 水の流れる方向1
(l) 水の流れる方向2
(m) 水の流れる方向3
(n) 水の流れる方向4
(o) 水の流れる方向5
(p) 水の流れる方向6
(q) 吐水口
(r) 電解電流制御部
(s) 電源部
(t) 流量センサー
(U) マイコン部
(v) スイッチング部A
(w) スイッチング部B
(X) 電源LED
(Y) 生成状態LED
(A) Plate electrode (electrode plate)
(B) Plate electrode (electrode plate)
(C) Plate electrode (electrode plate)
(D) Electrolytic cell (d-1) Inner wall of electrolytic cell (inner wall)
(E) Electrode plate fixing guide (f) Connection terminal (f-1) Connection terminal A
(F-2) Connection terminal B
(F-3) Connection terminal C
(A-1) Clearance between electrode plate (a) and electrode plate fixing guide (e) (b-1) Clearance between electrode plate (b) and electrode plate fixing guide (e) (c-1) Electrode plate ( c) Clearance between electrode plate fixing guide (e) (h) Upper end (i) Lower end (j) Water inlet IN side (k) Water flow direction 1
(L) Direction of water flow 2
(M) Direction of water flow 3
(N) Direction of water flow 4
(O) Direction of water flow 5
(P) Direction of water flow 6
(Q) Water outlet (r) Electrolytic current control unit (s) Power supply unit (t) Flow rate sensor (U) Microcomputer unit (v) Switching unit A
(W) Switching part B
(X) Power LED
(Y) Generation status LED

Claims (4)

水道水その他の被処理水を多電極型電解槽に導入し水質改善をおこなう電解水生成方法において、
槽内に複数の板状電極を離隔して並設し、隣接する電極間で陰陽電極を構成するとともに、上部槽端の側壁に入水口と吐水口を対向して設け、前記陰陽電極間を経由して被処理水を一方向に流通させ、かつ、該陰陽電極への印加極性を周期的又は間欠的に反転させながら被処理水の電気分解をおこなうことにより、水素ガス及び酸素ガスが混在した状態の電解水を生成するようにしたことを特徴とする電解水生成方法。
In the electrolyzed water generation method for improving the water quality by introducing tap water and other treated water into the multi-electrode electrolytic cell,
A plurality of plate-like electrodes are spaced apart from each other in the tank, and a yin / yang electrode is formed between adjacent electrodes, and a water inlet and a water outlet are provided on the side wall of the upper tank end to face each other between the yin and yang electrodes. Hydrogen gas and oxygen gas are mixed by circulating the water to be treated in one direction via the electrolysis and performing electrolysis of the water to be treated while periodically or intermittently reversing the polarity applied to the negative and positive electrodes. An electrolyzed water generating method characterized in that electrolyzed water in a state of being produced is generated.
槽内壁と最外設置電極との間隔を5mm以内に狭めることにより、電解水のpHを5.8〜8.6範囲に調整するようにした請求項1記載の電解水生成方法。   The method for generating electrolyzed water according to claim 1, wherein the pH of the electrolyzed water is adjusted to a range of 5.8 to 8.6 by narrowing the distance between the inner wall of the tank and the outermost electrode to within 5 mm. 水道水その他の被処理水を多電極型電解槽に導入し水質改善をおこなう電解水生成装置において、
上部側壁に入水口と吐水口を対設した電解槽と、
該電解槽の縦断方向に平面配置され、かつ、横断方向に離隔して対向設置された複数の板状電極から構成され、それぞれの電極の上下端のいずれかに水路をつなぐクリアランスを設け、かつ、設置内外方向に該クリアランスを上下に交互配置した陰陽電極と、
該陰陽電極への印加極性を周期的又は間欠的に反転させながら被処理水の電気分解をおこなうための極性反転回路を含む電解電流制御部を具備し、
前記陰陽電極間を水路として被処理水を一方向に流通させ、電解生成した水素ガス及び酸素ガスが混在した状態の電解水を取り出すようにしたことを特徴とする電解水生成装置。
In the electrolyzed water generator that improves the water quality by introducing tap water and other treated water into the multi-electrode electrolytic cell,
An electrolytic cell having a water inlet and a water outlet on the upper side wall;
It is composed of a plurality of plate-like electrodes arranged in a plane in the longitudinal direction of the electrolytic cell and opposed to each other in the transverse direction, and a clearance for connecting a water channel is provided at either the upper or lower end of each electrode; and , A positive and negative electrode alternately arranged above and below the clearance in the direction of installation inside and outside,
An electrolytic current control unit including a polarity reversing circuit for performing electrolysis of water to be treated while periodically or intermittently reversing the polarity applied to the yin and yang electrodes;
An electrolyzed water generating apparatus characterized in that the water to be treated is circulated in one direction between the yin and yang electrodes, and electrolyzed water in a state in which electrogenerated hydrogen gas and oxygen gas are mixed is taken out.
槽内壁と最外設置電極との間隔を5mm以内に狭めることにより、電解水のpHを5.8〜8.6範囲に調整するようにした請求項3記載の電解水生成装置。   The electrolyzed water generating apparatus according to claim 3, wherein the pH of the electrolyzed water is adjusted to a range of 5.8 to 8.6 by narrowing the distance between the inner wall of the tank and the outermost electrode to within 5 mm.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012005964A (en) * 2010-06-25 2012-01-12 Panasonic Electric Works Co Ltd Oxygen-enriched water generating apparatus
CN105217738A (en) * 2014-06-24 2016-01-06 罗民雄 A kind of method and apparatus having one or more water entrys also water inlet can be made brine electrolysis

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5335741B2 (en) * 2010-08-12 2013-11-06 株式会社テックコーポレーション Drinking electrolyzed water device using bottled water as raw water

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012005964A (en) * 2010-06-25 2012-01-12 Panasonic Electric Works Co Ltd Oxygen-enriched water generating apparatus
CN105217738A (en) * 2014-06-24 2016-01-06 罗民雄 A kind of method and apparatus having one or more water entrys also water inlet can be made brine electrolysis

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