JP4605694B2 - Water quality improvement method and electrolyzed water generating apparatus in electrolyzed water generation - Google Patents
Water quality improvement method and electrolyzed water generating apparatus in electrolyzed water generation Download PDFInfo
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本発明は、水道水その他の被処理水を電解槽に導入し、交流電解と活性炭ろ過による水の浄化を同時的に処理するようにした電解水生成における水質改善方法及び電解水生成装置に関する。 The present invention relates to a method for improving water quality and an electrolyzed water generating apparatus in electrolyzed water generation in which tap water and other water to be treated are introduced into an electrolytic cell to simultaneously treat water purification by AC electrolysis and activated carbon filtration.
従来、水道水などの水質を改善する機器として、活性炭でろ過す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機器が実用化されている。しかし、これらの機器は、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という問題があった。 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, devices that use magnets to improve the quality of water by applying magnetic field lines have been put into practical use. However, these devices are difficult to use for a long period of time, and the magnetic field lines that have a low "Gauss" indicating the strength of the magnet and those that use a ring-shaped inner side have a demagnetizing action and improve water quality. There was a problem of lack of the 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、アルカリ水と酸性水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。)。
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すべてが飲用でき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 unspecified consumers cannot drink.
また、この種のものでは、連続して水を電気分解している間に、電極板にカルシウム、マグネシウムなどが付着して電解能力が低下していくという問題があり、これを解決するために、一定時間の電気分解を行ったあと、電解槽の残水を排水するときに、電解極性を切り替えて(プラス極とマイナス極を反転)カルシウムやマグネシウムの付着を防ぐという洗浄方法(所謂、逆電解洗浄。)の提案があった(例えば特許文献2を参照。)。
しかしながら、生成終了後に極性を切り替えていた場合、生成時間と洗浄時間が同じでないと効果が弱く、通常電解時間の方が長時間使用されるため、完全な洗浄に至らないという問題がある。 However, when the polarity is switched after the generation is completed, the effect is weak unless the generation time and the cleaning time are the same, and the normal electrolysis time is used for a longer time, so that there is a problem that complete cleaning cannot be achieved.
こうしたなかで、一定時間電気分解を行った後、再び電気分解を行うときに、上記極性を反転させるか、吐水弁を反転させて、電気分解と洗浄を同時に行う方法の提案があった(例えば特許文献3を参照。)。
しかし、ここでも前回電気分解を行った時間と今回電気分解を行う時間は同じではなく、使用者が使用する頻度や使用時間により、電気分解の使用極性が偏ると言う問題があった。 However, here again, the time of the previous electrolysis and the time of the current electrolysis are not the same, and there is a problem that the use polarity of the electrolysis is biased depending on the frequency and time of use by the user.
また、電気分解槽においては、従来水流はまんべんなく電極板に均等に接触しないことから、水の道が出来て、電極板の寿命低下や電解能力の低下につながるという問題もあった。 Further, in the electrolysis tank, since the conventional water flow is not evenly contacted with the electrode plate evenly, there is a problem that a water path is formed, leading to a decrease in the life of the electrode plate and a decrease in electrolysis ability.
また、電気分解式の水質改善装置にあっては、電解槽と浄水槽は分割されており、最低二槽のスペース増大および、経済的に高額になっていた。 Moreover, in the electrolysis-type water quality improvement apparatus, the electrolytic cell and the water purification tank are divided, and the space of at least two tanks is increased and it is economically expensive.
そこで、電気分解中に電極表面に付着する、カルシウムやマグネシウムさらに水素と酸素の気泡などが、電解効率を低下させることを防ぎ、電気分解時の電流電圧を極間だけでなく、極内にも電流電圧を印加させて、水流を遮断することなく安定的に電気分解水を生成させ、原水のpHをアルカリ性や酸性にほとんど変えることなく、電解水を生成可能とすることが要請される。ここで、電解水は、被処理水(水道水)に含まれる不純物(特に塩素)を除去した浄水であることが望まれる。 Therefore, calcium, magnesium, and hydrogen and oxygen bubbles adhering to the electrode surface during electrolysis are prevented from lowering the electrolysis efficiency, and the current voltage during electrolysis is not only between the electrodes but also within the electrodes. It is required to generate electrolyzed water stably by applying a current voltage, without interrupting the water flow, and changing the pH of the raw water almost to alkaline or acidic. Here, the electrolyzed water is preferably purified water from which impurities (particularly chlorine) contained in the water to be treated (tap water) are removed.
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電解槽に導入し、交流電解と活性炭ろ過による水の浄化を同時的に処理するようにした電解水生成における水質改善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 water to be treated into an electrolytic cell, and simultaneously treats water purification by AC electrolysis and activated carbon filtration. The present invention provides a water quality improving method and an electrolyzed water generating device in electrolyzed water generation.
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円筒型電解槽に導入し、交流電解とろ過処理による浄化を同時的におこなう電解水生成における水質改善方法であって、直流電源に接続される陰陽電極の少なくとも一方を、円筒型圧縮活性炭からなる多孔質電極を形成して他方の電極に対して同心円上に配置し、被処理水を槽内導入して前記多孔質電極を通過させ、陰陽電極の印加極性を周期的又は間欠的に反転させながら電気分解をおこなうようにしたことを特徴とするものである。ここで、それぞれの陰陽電極に対して、数十kHz以上の高周波数と数Hz以上の低周波数からなる2種類の交流電流を適宜変調しながら重畳的に付加するように構成する場合がある。 In order to solve the problem, the present invention is a water quality improvement method in electrolyzed water generation in which tap water or other treated water is introduced into a cylindrical electrolytic cell, and purification by alternating current electrolysis and filtration is performed simultaneously. At least one of the yin and yang electrodes connected to the power source is formed with a porous electrode made of cylindrical compressed activated carbon and is arranged concentrically with respect to the other electrode. And the electrolysis is carried out while periodically or intermittently reversing the polarity applied to the yin and yang electrodes. Here, there may be a case where two types of alternating currents having a high frequency of several tens of kHz or more and a low frequency of several Hz or more are added to each of the yin and yang electrodes while being appropriately modulated.
また、水道水その他の被処理水を円筒型電解槽に導入し、交流電解とろ過処理による浄化を同時的におこなう電解水生成装置であって、
直流電源に接続される陰陽電極の少なくとも一方を、円筒型圧縮活性炭からなる多孔質電極を形成し、他方の電極に対して同心円上に配置するとともに、前記直流電源と陰陽電極間に、その印加極性を周期的又は間欠的に反転させる極性反転回路を有するとともに、それぞれの陰陽電極に対して、数十kHz以上の高周波数と数Hz以上の低周波数からなる2種類の交流電流を適宜変調しながら重畳的に付加する変調回路を含む電解電流制御手段を有してなり、被処理水を槽内導入し、前記多孔質電極を通過させながら交流電解をおこなうようにしたことを特徴とするものである。
Also, an electrolyzed water generating device that introduces tap water and other water to be treated into a cylindrical electrolytic cell, and performs purification by alternating current electrolysis and filtration treatment simultaneously,
At least one of the yin and yang electrodes connected to the dc power source forms a porous electrode made of cylindrical compressed activated carbon, and is disposed concentrically with respect to the other electrode, and the application between the dc power source and the yin and yang electrode It has a polarity inversion circuit that inverts the polarity periodically or intermittently, and appropriately modulates two types of alternating current consisting of a high frequency of several tens of kHz or more and a low frequency of several Hz or more for each negative and positive electrode. While having an electrolytic current control means including a modulation circuit that is added in a superimposed manner, water to be treated is introduced into the tank, and AC electrolysis is performed while passing through the porous electrode. It is.
この発明によれば、陰陽電極として、繊維状活性炭やヤシガラ活性炭とアクリル繊維などを加えて成型加工(賦型化)した圧縮活性炭からなる多孔質電極を用いることにより、ろ過フィルターを兼有することができる。 According to this invention, it is possible to have a filtration filter by using a porous electrode made of compressed activated carbon that is molded (shaped) by adding fibrous activated carbon or coconut shell activated carbon and acrylic fiber as the yin and yang electrode. it can.
また、この多孔質電極は、水に含まれる塩素などの不純物をろ過するとともに、水を電気分解して、酸化還元電位を低下させて、水の酸化を防ぐ。 In addition, this porous electrode filters impurities such as chlorine contained in water and electrolyzes water to lower the oxidation-reduction potential to prevent water oxidation.
さらに、電解水の生成を一時中断させること無く、生成中に印加極性のプラスとマイナスを連続して逆転させることで、電極を洗浄することが必要なくなる。そのため、電解水を連続して吐水することができる。 Furthermore, it is not necessary to clean the electrodes by continuously reversing the positive and negative polarity of the applied polarity during the generation without temporarily interrupting the generation of the electrolyzed water. Therefore, electrolyzed water can be discharged continuously.
しかも、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、尚且つ電極表面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, cleaning and electrolyzed water are equally generated regardless of the use time and frequency, and adhesion of calcium and magnesium and hydrogen and oxygen bubbles on the electrode surface can be prevented.
また、多孔質電極は多様な水路(活性炭孔)を作るので、電極間だけではなく、電極内においても電流が交差して電気分解がおこる。そのため、電解効率を上げることができる。 In addition, since the porous electrode forms various water channels (activated carbon holes), the current crosses not only between the electrodes but also within the electrodes, and electrolysis occurs. Therefore, the electrolytic efficiency can be increased.
さらに、製作費が安価になり、圧縮活性炭のろ過能力の寿命により、交換を定期的に行えることで、常に清潔になる。 In addition, production costs are reduced and the lifetime of the filtration capacity of the compressed activated carbon makes it possible to perform regular replacements so that it is always clean.
円筒型圧縮活性炭からなる多孔質電極は、繊維状活性炭やヤシガラ活性炭とアクリル繊維などを加えて成型加工(賦型化)したものに、非腐食性金属の電極端子を装着してなるものであり、ろ過フィルターと電極とを兼有する。 A porous electrode made of cylindrical compressed activated carbon is made by adding a non-corrosive metal electrode terminal to a molded activated carbon fiber or coconut shell activated carbon and acrylic fiber. The filter and the electrode are combined.
単筒形電極〔後述の実施例1〕を構成したものにおいては、陰陽電極の一方である多孔質電極の中空部(電解槽の中心)にステンレスやチタンなどの非腐食性金属素材からなる棒状または板状の金属電極を配置して陰陽電極の他方を形成し、多孔質電極の外側から被処理水を導入し、槽内中心部(金属電極側)へ滲透通過させながら、陰陽電極の印加極性を反転させる交流電解と活性炭ろ過を相乗的に施して、電解水の浄化生成を増補するようにしている。
In the case of constituting a single cylindrical electrode [
陰陽電極には、極性反転回路を介して直流電源にコード接続する。通常、直流電流0.1A以上(直流電圧1V以上)を通電し、電解水の生成を遮断することなく極性反転回路を介して一定の間隔で印加極性を反転させるので(交流電解)、連続運転によっても、直流電解の場合に不可避的に発生する電極汚染の心配がない。 The yin and yang electrode is connected to a DC power source through a polarity inversion circuit. Normally, a direct current of 0.1 A or higher (DC voltage of 1 V or higher) is applied, and the applied polarity is reversed at regular intervals via a polarity reversal circuit without interrupting the generation of electrolyzed water (AC electrolysis), so continuous operation However, there is no fear of electrode contamination that inevitably occurs in the case of direct current electrolysis.
なお、陰陽電極間には、互いに接触しないように多孔質電極に内接してコア材(隔壁)を設けている。好適なコア材は樹脂製の多孔性パイプであって、筒状壁面に多数の通水孔を形成したものである。 In addition, between the yin and yang electrodes, a core material (partition wall) is provided in contact with the porous electrodes so as not to contact each other. A suitable core material is a porous pipe made of resin, in which a large number of water passage holes are formed on a cylindrical wall surface.
また、多重筒形電極〔後述の実施例2〕を構成したものにおいては、円筒型電解槽の同心円上放射方向に上記同様の多孔質電極を隔壁を介して多重配置して陰陽電極を交互形成する。 In addition, in the case of a multi-cylindrical electrode [Example 2 described later], a plurality of porous electrodes similar to the above are arranged in a concentric radial direction of a cylindrical electrolytic cell through a partition wall to alternately form yin and yang electrodes. To do.
至適には、上記構成のそれぞれの多孔質電極に対して、数十kHz以上の高周波数と数Hz以上の低周波数からなる2種類の交流電流を適宜変調しながら重畳的に付加する。これにより、多孔質電極内を通過する被処理水はこの影響(変調電界)を受けることになる。装置構成上、図5に電解電流制御制御系統を説明するブロック図を示すとおり、変調回路を含む電解電流制御手段〔後述の図5中、符号(r)〕をマイコン〔後述の図5中、符号(U)〕に搭載している。 Optimally, two types of alternating currents having a high frequency of several tens of kHz or more and a low frequency of several Hz or more are added in a superimposed manner to each of the porous electrodes having the above-described configuration while appropriately modulating them. Thereby, the to-be-processed water which passes the inside of a porous electrode receives this influence (modulation electric field). As shown in the block diagram for explaining the electrolytic current control system in FIG. 5, the electrolytic current control means including a modulation circuit [in FIG. 5 described later, symbol (r)] is replaced with the microcomputer [in FIG. [Usage (U)].
そして、塩素などの不純物をろ過しながら電解を行い酸化還元電位を低下させ水の酸化を防止するとともに、電解中に電極表面に付着する、カルシウムやマグネシウムさらに水素と酸素の気泡などで、電解効率を低下させることを防ぐようにしている。また、電極面積が広いので、水流を遮断することなく安定的に電解水を生成することができるという利点もある。 Electrolysis is performed while impurities such as chlorine are filtered to reduce the oxidation-reduction potential to prevent water oxidation, and the electrolytic efficiency is reduced by the bubbles of calcium, magnesium, and hydrogen and oxygen that adhere to the electrode surface during electrolysis. It is trying to prevent lowering. Moreover, since the electrode area is large, there is also an advantage that electrolyzed water can be stably generated without blocking the water flow.
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、単筒形電極を構成した実施例装置(以下、単筒形装置。)の断面視説明図である。 FIG. 1 is a cross-sectional explanatory view of an embodiment apparatus (hereinafter referred to as a single cylinder apparatus) configured with a single cylinder electrode.
図2は、単筒形装置の平面視説明図である。 FIG. 2 is an explanatory view in plan view of the single cylindrical device.
図示するように、単筒形装置(X)は、繊維状活性炭および/またはヤシガラ活性炭と、アクリル繊維その他の帯電性繊維とを成形材料として賦型化し、かつ、非腐食性金属素材からなる棒状又は板状の電極端子(c)を挿設した多孔質電極(a)と、円筒型電解槽(f)の中心に非腐食性の金属電極(b)を配置するとともに、その同心円上に多孔質電極(a)を離隔保持して単筒形電極(a)(b)を構成したものであり、該単筒形電極(a)(b)の外側に被処理水を槽内導入し、内側の中空部(後述のe)へ通過させて浄化生成した電解水を取り出すようにしたものである。 As shown in the figure, the single cylindrical device (X) is a rod-shaped device made of a non-corrosive metal material formed from a fibrous activated carbon and / or coconut shell activated carbon and an acrylic fiber or other chargeable fiber as a molding material. Alternatively, a porous electrode (a) with a plate-like electrode terminal (c) inserted therein and a non-corrosive metal electrode (b) at the center of the cylindrical electrolytic cell (f) are disposed on a concentric circle. The single electrode (a) (b) is configured by holding the porous electrode (a) separately, and water to be treated is introduced into the tank outside the single tube electrode (a) (b), Electrolyzed water that has been purified by passing through the inner hollow portion (e described later) is taken out.
ここで、離隔保持は隔壁の介設であって、多孔質電極(a)にコア材を内接するものである。コア材(後述のd)の筒状壁面には多数の通水孔を形成している。 Here, the separation holding is an interposition of the partition wall, and the core material is inscribed in the porous electrode (a). A large number of water passage holes are formed on the cylindrical wall surface of the core material (described later).
電解槽は内部が空洞になっている浄水シリンダー(f)として形成され、その側壁に原水(被処理水)のIN側注水口(10)を形設し、内部に円筒型圧縮活性炭からなる多孔質電極(a)を収設している。 The electrolytic cell is formed as a water purification cylinder (f) having a hollow inside, and an IN-side water injection port (10) for raw water (treated water) is formed on the side wall of the electrolytic cell. A quality electrode (a) is provided.
さらに、多孔質電極(a)内側の中空部(電解槽の中心)には、非腐食性の金属電極(b)を立設しており、これら電極(a)(b)間は、接触を避けるために離隔配置(保持)されている。ここで、離隔保持は、多孔質電極(a)の内壁に、円筒形のコア材(d)を内接して隔壁を形成するのが好ましい。具体的には、繊維状、網目状、多数の通水孔を有した非腐食性金属又は樹脂製の多孔性パイプ(d)を設ける。 Furthermore, a non-corrosive metal electrode (b) is erected in the hollow part (center of the electrolytic cell) inside the porous electrode (a), and contact between these electrodes (a) and (b) is prevented. It is spaced apart (held) to avoid it. Here, it is preferable that the separation is maintained by inscribed a cylindrical core material (d) on the inner wall of the porous electrode (a) to form a partition wall. Specifically, a porous pipe (d) made of a non-corrosive metal or resin having a fibrous shape, a mesh shape, and a large number of water passage holes is provided.
この多孔性パイプ(d)の筒壁の厚みは薄くなっていて、筒内(内空間)は排水ガイド(e)を形設する。浄化生成した電解水を通過させて、OUT側送水口(11)へ誘導するためである。 The thickness of the cylindrical wall of the porous pipe (d) is thin, and the drainage guide (e) is formed in the cylinder (inner space). This is because the purified and generated electrolyzed water is allowed to pass and guided to the OUT side water supply port (11).
そこで、まず原水(被処理水)はIN側注水口(10)から浄水シリンダー内(f)へ注水され、図2中の矢印(g)方向に向って被処理水が移動(滲透通過)する。 Therefore, first, the raw water (treated water) is poured from the IN side water inlet (10) into the water purification cylinder (f), and the treated water moves (permeates through) in the direction of the arrow (g) in FIG. .
このとき、多孔質電極(a)を通過するとき、水に含まれる塩素や不純物が除去されながら、金属電極(b)に印加された電流・電圧の影響を受ける。 At this time, when passing through the porous electrode (a), it is affected by the current and voltage applied to the metal electrode (b) while removing chlorine and impurities contained in the water.
さらに、多孔質電極(a)を通過した被処理水は、金属電極(b)側に移動して、浄化生成した電解水となる。 Furthermore, the to-be-processed water which passed the porous electrode (a) moves to the metal electrode (b) side, and becomes purified electrolyzed water.
そして、コア材(多孔性パイプd)の内空間である排水ガイド(e)を通り、OUT側(11)へ排水される。 And it drains to the OUT side (11) through the drainage guide (e) which is the inner space of the core material (porous pipe d).
ここで、多孔質電極(a)と金属電極(b)には直流電源(s)から直流電流0.2〜1.5A(直流電圧5〜36V)が印加され、かつ、この陰陽電極(a)(b)は、極性反転回路(14)により、一定時間ごとに印加極性を反転可能に構成している。 Here, a direct current of 0.2 to 1.5 A (DC voltage of 5 to 36 V) is applied to the porous electrode (a) and the metal electrode (b) from the DC power source (s), and the negative and positive electrodes (a (B) is configured such that the polarity can be reversed at regular intervals by the polarity reversing circuit (14).
また、マイコン(U)に搭載した変調回路を含む電解電流制御手段(r)を介して、数十kHz以上の高周波数と数Hz以上の低周波数からなる2種類の交流電流を適宜変調しながら重畳的に付加するようにしている。これにより、多孔質電極(a)には高周波数と低周波数が印加交差し、内部の活性炭孔には、電磁界が発生している。 In addition, while appropriately modulating two types of alternating currents consisting of a high frequency of several tens of kHz or more and a low frequency of several Hz or more via an electrolytic current control means (r) including a modulation circuit mounted on the microcomputer (U). They are added in a superimposed manner. Thereby, a high frequency and a low frequency are applied to the porous electrode (a), and an electromagnetic field is generated in the activated carbon hole inside.
したがって、被処理水が(g)の方向に流れ、多孔質電極(a)内部を通過するとき、印加された高周波及び低周波の影響を受け、水の分子が激しく振動を起こす。 Therefore, when the water to be treated flows in the direction (g) and passes through the inside of the porous electrode (a), the water molecules are vigorously vibrated under the influence of the applied high frequency and low frequency.
また、多孔質電極(a)と金属電極(b)との間では水の電気分解が起こり水素イオン、水酸化イオンを生成する。 Further, water is electrolyzed between the porous electrode (a) and the metal electrode (b) to generate hydrogen ions and hydroxide ions.
さらに、被処理水が多孔質電極(a)の活性炭孔を通過するとき、高周波と低周波の影響を受け、電解水はさらに還元力が高く、分子集団の小さい水へと変化する。 Furthermore, when the water to be treated passes through the activated carbon pores of the porous electrode (a), it is affected by high and low frequencies, and the electrolyzed water has a higher reducing power and changes to water with a small molecular group.
本発明の他の実施例を添付図面を参照して以下説明する。実施例1記載の単筒形装置と同一の構成要素については同一符号を付した。 Another embodiment of the present invention will be described below with reference to the accompanying drawings. Constituent elements that are the same as those of the single cylinder apparatus described in the first embodiment are denoted by the same reference numerals.
図3は、多重筒形電極を構成した実施例装置(以下、多重筒形装置。)の断面視説明図である。 FIG. 3 is a cross-sectional explanatory view of an embodiment device (hereinafter referred to as a “multi-tubular device”) having a multi-tubular electrode.
図4は、多重筒形装置の平面視説明図である。図中の矢印(k)は被処理水の流れ方向を示す。 FIG. 4 is an explanatory diagram in plan view of the multiple cylindrical device. The arrow (k) in the figure indicates the flow direction of the water to be treated.
図示するように、多重筒形装置(Y)は、繊維状活性炭および/またはヤシガラ活性炭と、アクリル繊維その他の帯電性繊維とを成形材料として賦型化し、かつ、非腐食性金属素材からなる棒状又は板状の電極端子(c)を挿設した多孔質電極(a)を、円筒型電解槽の中心から放射方向同心円上に隔壁を介して多重配置して多重筒形電極(a,a')を構成したものであり、該多重筒形電極(a,a')の最外筒の外側に被処理水を槽内導入し、最内筒の内側の中空部へ通過させて浄化生成した電解水を取り出すようにしたものである。図示の多重筒形装置は、2重筒構成であるが、3重筒形や5重筒形に構成する場合がある。 As shown in the figure, the multi-cylindrical device (Y) is a rod-shaped device made of a non-corrosive metal material formed from a fibrous activated carbon and / or coconut shell activated carbon and an acrylic fiber or other charging fiber as a molding material. Alternatively, a porous electrode (a) having a plate-like electrode terminal (c) inserted therein is arranged in a multiplex manner on the radial concentric circle from the center of the cylindrical electrolytic cell via a partition wall, and multiple cylindrical electrodes (a, a ′ The water to be treated is introduced into the tank outside the outermost cylinder of the multi-tubular electrode (a, a ') and passed through the hollow part inside the innermost cylinder for purification. Electrolyzed water is taken out. The illustrated multiple cylinder device has a double cylinder configuration, but may be configured in a triple cylinder shape or a five cylinder shape.
ここで、隔壁は絶縁性コア材(d)であって筒状壁面に多数の通水孔を形成したものであり、好適には樹脂性の多孔性パイプを用いる。コア材(多孔性パイプd)を各多孔質電極(a,a')に内接し、電極(a,a')間の非接触を確保する。 Here, the partition wall is an insulating core material (d) having a large number of water passage holes formed on a cylindrical wall surface, and preferably a resinous porous pipe is used. A core material (porous pipe d) is inscribed in each porous electrode (a, a ′) to ensure non-contact between the electrodes (a, a ′).
最内筒の内側の中空部が排出ガイド(e)である。 A hollow portion inside the innermost cylinder is a discharge guide (e).
なお、個々の多孔質電極(a,a')の構成は、実施例1の単筒形装置におけるものと同様である。 The configuration of each porous electrode (a, a ′) is the same as that in the single-cylinder apparatus of the first embodiment.
(a)多孔質電極〔円筒型圧縮活性炭電極〕
(a')多孔質電極〔円筒型圧縮活性炭電極〕
(b)金属電極
(c)電極端子
(d)多孔性パイプ〔コア材〕
(e)排水ガイド
(f)浄水シリンダー〔電解槽〕
(g)水の流れる方向
(k)水の流れる方向
(10)IN側注水口
(11)OUT側注水口
(12)送電コード
(13)送電コード
(14)極性反転回路(スイッチング部A)
(s)直流電源部
(r)変調回路〔電解電流制御手段〕
(U)マイコン
(X)単筒形装置(第1実施例装置)
(Y)多重筒形装置(第2実施例装置)
(A) Porous electrode [cylindrical compressed activated carbon electrode]
(A ') Porous electrode [cylindrical compressed activated carbon electrode]
(B) Metal electrode (c) Electrode terminal (d) Porous pipe [core material]
(E) Drainage guide (f) Water purification cylinder [electrolyzer]
(G) Direction of water flow (k) Direction of water flow (10) IN side water inlet (11) OUT side water inlet (12) Power transmission cord (13) Power transmission cord (14) Polarity inversion circuit (switching unit A)
(S) DC power supply (r) modulation circuit [electrolytic current control means]
(U) Microcomputer (X) Single cylinder device (first embodiment device)
(Y) Multiple cylindrical apparatus (second embodiment apparatus)
Claims (7)
直流電源に接続される陰陽電極の少なくとも一方を、円筒型圧縮活性炭からなる多孔質電極を形成し、他方の電極に対して同心円上に配置し、被処理水を槽内導入して前記多孔質電極を通過させ、前記陰陽電極の印加極性を周期的又は間欠的に反転させながら電気分解をおこない、かつ、それぞれの陰陽電極に対して、数十kHz以上の高周波数と数Hz以上の低周波数からなる2種類の交流電流を適宜変調しながら重畳的に付加するようにしたことを特徴とする電解水生成における水質改善方法。 Water quality improvement method in electrolyzed water generation in which tap water or other treated water is introduced into a cylindrical electrolytic cell and purification by alternating current electrolysis and filtration treatment is performed simultaneously.
At least one of the yin and yang electrodes connected to the DC power source is formed with a porous electrode made of cylindrical compressed activated carbon, and is disposed concentrically with respect to the other electrode. Electrodes are passed through the electrodes and the polarity applied to the yin and yang electrodes is reversed periodically or intermittently , and for each yin and yang electrode, a high frequency of several tens of kHz or more and a low frequency of several Hz or more A method for improving water quality in electrolyzed water generation, characterized in that two types of alternating currents are added in a superimposed manner while being appropriately modulated.
円筒型電解槽の中心に非腐食性の金属電極を配置するとともに、その同心円上に前記多孔質電極を離隔保持して単筒形電極を構成したものであり、該単筒形電極の外側に被処理水を槽内導入し、内側の中空部へ通過させて浄化生成した電解水を取り出すようにした請求項1記載の電解水生成における水質改善方法。 Porous electrode is made of fibrous activated carbon and / or coconut shell activated carbon and acrylic fiber or other chargeable fiber as molding material, and rod-shaped or plate-shaped electrode terminals made of non-corrosive metal material are inserted. And
A non-corrosive metal electrode is arranged in the center of the cylindrical electrolytic cell, and the porous electrode is separated and held on a concentric circle to constitute a single cylindrical electrode, and outside the single cylindrical electrode. the treated water is introduced in the tank, the water quality improving method in the electrolytic water generation according to claim 1, wherein they were taken out of the electrolytic water generated purified by passing through the interior of the part.
円筒型電解槽の中心から放射方向同心円上に前記多孔質電極を隔壁を介して多重配置して多重筒形電極を構成したものであり、該多重筒形電極の最外筒の外側に被処理水を槽内導入し、最内筒の内側の中空部へ通過させて浄化生成した電解水を取り出すようにした請求項1記載の電解水生成における水質改善方法。 Porous electrode is made of fibrous activated carbon and / or coconut shell activated carbon and acrylic fiber or other chargeable fiber as molding material, and rod-shaped or plate-shaped electrode terminals made of non-corrosive metal material are inserted. And
A multi-tubular electrode is configured by arranging the porous electrodes in multiple radial concentric circles from the center of the cylindrical electrolytic cell via partition walls, and the outer side of the outermost cylinder of the multi-tubular electrode is processed. The method for improving water quality in electrolyzed water production according to claim 1 , wherein water is introduced into the tank and the electrolyzed water purified and produced by passing it through a hollow portion inside the innermost cylinder is taken out.
直流電源に接続される陰陽電極の少なくとも一方を、円筒型圧縮活性炭からなる多孔質電極を形成し、他方の電極に対して同心円上に配置するとともに、陰陽電極の印加極性を周期的又は間欠的に反転させる極性反転回路を有するとともに、それぞれの陰陽電極に対して、数十kHz以上の高周波数と数Hz以上の低周波数からなる2種類の交流電流を適宜変調しながら重畳的に付加する変調回路を含む電解電流制御手段を有してなり、被処理水を槽内導入し、前記多孔質電極を通過させながら交流電解をおこなうようにしたことを特徴とする電解水生成装置。 An electrolyzed water generating device that introduces tap water and other treated water into a cylindrical electrolytic cell, and performs purification by alternating current electrolysis and filtration treatment simultaneously,
At least one of the yin and yang electrodes connected to the direct current power source is formed as a porous electrode made of cylindrical compressed activated carbon and is arranged concentrically with respect to the other electrode, and the polarity of the yin and yang electrode is changed periodically or intermittently. Modulation that has a polarity reversal circuit that inverts the signal and adds two types of alternating currents of a high frequency of several tens kHz or more and a low frequency of several Hz or more to each of the negative and positive electrodes while appropriately modulating them. An electrolyzed water generating apparatus comprising electrolysis current control means including a circuit, wherein water to be treated is introduced into a tank and AC electrolysis is performed while passing through the porous electrode.
円筒型電解槽の中心に非腐食性の金属電極を配置するとともに、その同心円上に前記多孔質電極を離隔保持して単筒形電極を構成したものであり、該単筒形電極の外側に被処理水を槽内導入し、内側の中空部へ通過させて浄化生成した電解水を取り出すようにした請求項4記載の電解水生成装置。 A rod-shaped or plate-shaped porous electrode made of cylindrical compressed activated carbon is formed from fibrous activated carbon and / or coconut husk activated carbon and acrylic fiber or other chargeable fiber as a molding material, and made of a non-corrosive metal material. The electrode terminal is inserted and
A non-corrosive metal electrode is arranged in the center of the cylindrical electrolytic cell, and the porous electrode is separated and held on a concentric circle to constitute a single cylindrical electrode, and outside the single cylindrical electrode. The electrolyzed water generating apparatus according to claim 4 , wherein the water to be treated is introduced into the tank, and the electrolyzed water purified and generated by passing the water into the inner hollow portion is taken out.
円筒型電解槽の中心から放射方向同心円上に前記多孔質電極を隔壁を介して多重配置して多重筒形電極を構成したものであり、該多重筒形電極の最外筒の外側に被処理水を槽内導入し、最内筒の内側の中空部へ通過させて浄化生成した電解水を取り出すようにした請求項4記載の電解水生成装置。 Porous electrode is formed with fibrous activated carbon and / or coconut shell activated carbon and acrylic fiber or other chargeable fiber as a molding material, and a rod-shaped or plate-shaped electrode terminal made of a non-corrosive metal material is inserted. And
A multi-tubular electrode is configured by arranging the porous electrodes in multiple radial concentric circles from the center of the cylindrical electrolytic cell via partition walls, and the outer side of the outermost cylinder of the multi-tubular electrode is processed. 5. The electrolyzed water generating device according to claim 4 , wherein water is introduced into the tank and the purified electrolyzed water is taken out by passing it through a hollow portion inside the innermost cylinder.
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000033379A (en) * | 1998-07-16 | 2000-02-02 | Sanyo Electric Co Ltd | Electrolytic sterilizer |
JP2000263050A (en) * | 1999-03-23 | 2000-09-26 | Igaden:Kk | Method and apparatus for wastewater treatment |
JP2001123288A (en) * | 1999-10-27 | 2001-05-08 | Tsukishima Kikai Co Ltd | Electrolytic apparatus |
JP2001187382A (en) * | 2000-01-05 | 2001-07-10 | Art Foods:Kk | Water purifier for producing reduced water |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3206819B2 (en) * | 1991-07-26 | 2001-09-10 | コニカ株式会社 | Electrochemical treatment method for water to be treated |
JP3267779B2 (en) * | 1993-12-08 | 2002-03-25 | 大阪瓦斯株式会社 | Electrochemical sterilizer and sterilization method using the same |
-
2004
- 2004-03-30 JP JP2004099720A patent/JP4605694B2/en not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000033379A (en) * | 1998-07-16 | 2000-02-02 | Sanyo Electric Co Ltd | Electrolytic sterilizer |
JP2000263050A (en) * | 1999-03-23 | 2000-09-26 | Igaden:Kk | Method and apparatus for wastewater treatment |
JP2001123288A (en) * | 1999-10-27 | 2001-05-08 | Tsukishima Kikai Co Ltd | Electrolytic apparatus |
JP2001187382A (en) * | 2000-01-05 | 2001-07-10 | Art Foods:Kk | Water purifier for producing reduced water |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2016134619A1 (en) * | 2015-02-26 | 2016-09-01 | 罗民雄 | New method for controlling electrolyzed-water performance by using two sets of electrolytic electrode assemblies |
WO2016134618A1 (en) * | 2015-02-26 | 2016-09-01 | 罗民雄 | New method for membrane-free electrolysis of water capable of controlling acid-base property of the electrolysed water |
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