JP2012115749A - Electrolytic apparatus for making hypochlorous acid water, and method for making hypochlorous acid water - Google Patents

Electrolytic apparatus for making hypochlorous acid water, and method for making hypochlorous acid water Download PDF

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JP2012115749A
JP2012115749A JP2010266679A JP2010266679A JP2012115749A JP 2012115749 A JP2012115749 A JP 2012115749A JP 2010266679 A JP2010266679 A JP 2010266679A JP 2010266679 A JP2010266679 A JP 2010266679A JP 2012115749 A JP2012115749 A JP 2012115749A
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hypochlorous acid
acid water
hydrochloric acid
electrolytic cell
dilute hydrochloric
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JP5711945B2 (en
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Mamoru Tomita
守 冨田
Yukihiro Tomita
幸裕 冨田
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Dairy Techno Inc
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Dairy Techno Inc
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Abstract

PROBLEM TO BE SOLVED: To provide an electrolytic apparatus for making hypochlorous acid water suitable for sterilization and not low in pH, and a method for making hypochlorous acid water.SOLUTION: The electrolytic apparatus is constituted of an electrolytic tank 1 for receiving the supply of dilute hydrochloric acid from the lower part thereof, the anode plate 2a and cathode plate 2b provided in the electrolytic tank 1 in opposed relationship and having opposed inner surfaces and the outer surfaces on the sides opposite to the inner surfaces enabling the contact with dilute hydrochloric acid and a current quantity adjusting device 11 for adjusting the electric current to both electrode plates 2a and 2b so that the whole of dilute hydrochloric acid supplied from the lower part of the electrolytic tank 1 is electrolyzed by both electrode plates 2a and 2b to make hypochlorous acid water to thereby allow the same to flow out from the upper part of the electrolytic tank 1.

Description

本発明は殺菌水として有効な次亜塩素酸水の生成用の電解装置及び次亜塩素酸水の生成方法に関する。   The present invention relates to an electrolyzer for producing hypochlorous acid water effective as sterilizing water and a method for producing hypochlorous acid water.

従来の次亜塩素酸水の電解装置として、図4に示すように、内壁に互いに平行に対峙して配設した陽極板aと陰極板bとを有する電解槽cに、食塩及び塩酸を少量含む電解添加液を送り、前記電解槽c内で電気分解して、生成した次亜塩素酸及び希塩酸を混合槽dで水を加えて希釈して、次亜塩素酸水を得るようにしたものが知られている(特許文献1参照)。   As a conventional hypochlorous acid electrolyzer, as shown in FIG. 4, a small amount of sodium chloride and hydrochloric acid are added to an electrolytic cell c having an anode plate a and a cathode plate b arranged in parallel with each other on the inner wall. Electrolyte containing electrolytic solution is sent, electrolyzed in the electrolytic cell c, and the produced hypochlorous acid and diluted hydrochloric acid are diluted by adding water in the mixing vessel d to obtain hypochlorous acid water. Is known (see Patent Document 1).

特開平9−122651号公報JP-A-9-122651

しかしながら、このような従来の電解装置は、通常、該電解槽c内に供給した希塩酸の全部を電気分解できないので、この電気分解されなかった希塩酸により、生成した次亜塩素酸水のpHが低い値となり、この次亜塩素酸水の中和のためにカルシウムなどを含む硬度の高い水が必要であるという問題があった。   However, such a conventional electrolyzer usually cannot electrolyze all of the dilute hydrochloric acid supplied into the electrolytic cell c, so that the pH of the hypochlorous acid water produced by the dilute hydrochloric acid not electrolyzed is low. There was a problem that water with high hardness containing calcium and the like was required for neutralization of this hypochlorous acid water.

本発明はこれらの問題点を解消し、電解槽内に供給された希塩酸の全部を電気分解できる次亜塩素酸水生成用電解装置及び次亜塩素酸水の生成方法を提供することを目的とする。   An object of the present invention is to solve these problems and to provide an electrolyzer for generating hypochlorous acid water and a method for generating hypochlorous acid water capable of electrolyzing all of dilute hydrochloric acid supplied into the electrolytic cell. To do.

前記の目的を達成すべく、第1発明は次亜塩素酸水生成用電解装置に関し、下部から希塩酸が供給される電解槽と、該電解槽内に対向して設けられ対向する内表面とその反対側の外表面に希塩酸が接触可能な陽極板及び陰極板と、これら両電極板により前記下部から供給される希塩酸の全部を電気分解して次亜塩素酸水を生成し前記電解槽の上部より次亜塩素酸水が流出するように前記両電極板への電流を調整する電流量調整装置とからなり、又第2発明は次亜塩素酸水の生成方法に関し、対向する内表面とその反対側の外表面において電気分解可能な陽極板及び陰極板を有する電解槽に希塩酸を該電解槽の下部より供給し、該電解槽内に供給される希塩酸の全部を電気分解して次亜塩素酸水を生成し、前記両電極板への電流を調整して前記電解槽の上部から次亜塩素酸水を流出するようにした。   In order to achieve the above-mentioned object, the first invention relates to an electrolyzer for generating hypochlorous acid water, an electrolyzer to which dilute hydrochloric acid is supplied from the lower part, an inner surface opposed to and provided in the electrolyzer, and its An anode plate and a cathode plate that can be contacted with dilute hydrochloric acid on the outer surface on the opposite side, and the dilute hydrochloric acid supplied from the lower part by electrolysis of all of the dilute hydrochloric acid by these electrode plates to generate hypochlorous acid water, and the upper part of the electrolytic cell The second invention relates to a method for producing hypochlorous acid water, and an inner surface facing the same, and a method for adjusting the amount of current to both the electrode plates so that hypochlorous acid water flows out. Dilute hydrochloric acid is supplied from the lower part of the electrolytic cell to the electrolytic cell having an anode plate and a cathode plate that can be electrolyzed on the outer surface on the opposite side, and all of the diluted hydrochloric acid supplied into the electrolytic cell is electrolyzed to hypochlorite. Generate acid water, adjust the current to both electrode plates And from the top of the solution tank to flow out of the hypochlorous acid solution.

本発明によれば、電解槽内に供給された希塩酸のうち未分解の希塩酸がないので、生成した次亜塩素酸水のpHが中性付近を示し、次亜塩素酸水の中和のためにカルシウムなどを含む硬度の高い水を必要としない。   According to the present invention, since there is no undecomposed dilute hydrochloric acid among the dilute hydrochloric acid supplied into the electrolytic cell, the pH of the produced hypochlorous acid water is in the vicinity of neutrality, and the hypochlorous acid water is neutralized. It does not require water with high hardness including calcium.

また、両電極板の内表面のみならず外表面に供給された希塩酸も電気分解に寄与されるので電流効率を上げることができる。   Moreover, since dilute hydrochloric acid supplied not only to the inner surfaces of both electrode plates but also to the outer surface contributes to electrolysis, the current efficiency can be increased.

本発明の次亜塩素酸水生成用の電解装置の実施例1の管路図である。It is a pipe line figure of Example 1 of the electrolyzer for hypochlorous acid water production | generation of this invention. 図1のII−II線截断面図である。FIG. 2 is a cross-sectional view taken along line II-II in FIG. 1. 本発明の次亜塩素酸水生成用の電解装置の電解槽の実施例2の縦断正面図である。It is a vertical front view of Example 2 of the electrolytic cell of the electrolyzer for hypochlorous acid water production | generation of this invention. 従来の次亜塩素酸水生成用の電解装置の管路図である。It is a pipeline diagram of the conventional electrolyzer for hypochlorous acid water production | generation.

本発明を実施するための形態の実施例を以下に示す。   The example of the form for carrying out the present invention is shown below.

本発明の次亜塩素酸水生成用電解装置の実施例1を図1及び図2により説明する。   Example 1 of an electrolyzer for generating hypochlorous acid water according to the present invention will be described with reference to FIGS.

図1において、1は電解槽を示し、該電解槽1は、その内部に矩形状の陽極板2aと矩形状の陰極板2bとが対向して設けられており、該陽極板2a及び該陰極板2bは、対向する内表面とその反対側の外表面において電気分解が可能に露出して形成されている。   In FIG. 1, reference numeral 1 denotes an electrolytic cell. The electrolytic cell 1 is provided with a rectangular anode plate 2a and a rectangular cathode plate 2b facing each other. The anode plate 2a and the cathode The plate 2b is formed to be exposed so as to be electrolyzed on the opposing inner surface and the opposite outer surface.

3は希塩酸タンクを示し、該希塩酸タンク3は、例えば、約3%濃度の希塩酸が貯留され、また、該希塩酸タンク3と前記電解槽1の下部である底部1aとの間に送水管4が連結されていると共に、該送水管4に希塩酸供給ポンプ5が介在されており、該希塩酸供給ポンプ5の駆動により前記希塩酸タンク3内の希塩酸を前記電解槽1内に供給するようにした。   Reference numeral 3 denotes a dilute hydrochloric acid tank. The dilute hydrochloric acid tank 3 stores, for example, about 3% dilute hydrochloric acid, and a water pipe 4 is provided between the dilute hydrochloric acid tank 3 and the bottom 1a which is the lower part of the electrolytic cell 1. In addition, a dilute hydrochloric acid supply pump 5 is interposed in the water supply pipe 4, and the dilute hydrochloric acid tank 3 is supplied into the electrolytic cell 1 by driving the dilute hydrochloric acid supply pump 5.

6は貯留タンク、7は循環管路を示し、該循環管路7はその流入管部7aと流出管部7bにおいて前記貯留タンク6に接続すると共に、該循環管路7の中間部に循環ポンプ8を介在し、該循環ポンプ8の駆動により、前記貯留タンク6内の水が前記流入管部7aから流入して前記循環管路7内を流動し前記流出管路7bより前記貯留タンク6内に流出し、前記循環管路7内を水又は次亜塩素酸水が循環するようにした。   Reference numeral 6 denotes a storage tank, and 7 denotes a circulation pipe. The circulation pipe 7 is connected to the storage tank 6 at an inflow pipe portion 7a and an outflow pipe portion 7b, and a circulation pump is provided at an intermediate portion of the circulation pipe 7 8, the water in the storage tank 6 flows from the inflow pipe portion 7a and flows in the circulation pipe 7 by driving the circulation pump 8, and flows into the storage tank 6 from the outflow pipe 7b. The water or hypochlorous acid water was circulated in the circulation pipe 7.

9は混入管路を示し、該混入管路9は、前記電解槽1の上部である蓋部1bに貫通して形成されていると共に、該混入管路9の流出端部が前記循環管路7の中間部に連通接続して、その連通接続した混入箇所Aにおいて、前記電解槽1内で生成し該混入管路9からの次亜塩素酸水を、前記循環管路7内を流動する水又は次亜塩素酸水に混入するようにした。   Reference numeral 9 denotes a mixing pipe line. The mixing pipe line 9 is formed so as to penetrate through the lid portion 1b which is the upper part of the electrolytic cell 1, and the outflow end of the mixing pipe line 9 is the circulation pipe line. 7 is connected to the intermediate portion 7 and the hypochlorous acid water generated in the electrolytic cell 1 and flowing from the mixing pipe 9 flows in the circulation pipe 7 at the mixing point A that is connected and connected. It mixed with water or hypochlorous acid water.

10は貯留タンク6の排出管を示す。   Reference numeral 10 denotes a discharge pipe of the storage tank 6.

11は前記陽極板2aと陰極板2bにリード線を介して接続される電流量調整装置を示し、該電流量調整装置11は、前記電解槽1内に供給された希塩酸の全部が、該電解槽1の下部から上部に上昇して前記混入管路9内に流入されるまでに、下記の数1の反応式に基づき電気分解される電流量を前記両電極板2a,2bに通電する。   Reference numeral 11 denotes a current amount adjusting device connected to the anode plate 2a and the cathode plate 2b via a lead wire. The current amount adjusting device 11 is configured so that all of the diluted hydrochloric acid supplied into the electrolytic cell 1 is electrolyzed. A current amount that is electrolyzed based on the following reaction formula 1 is supplied to both the electrode plates 2a and 2b from the lower part of the tank 1 to the upper part and flowing into the mixing pipe 9.

(数1)
2HCl+HO→HCl+HClO+H
(Equation 1)
2HCl + H 2 O → HCl + HClO + H 2

また、前記貯留タンク6には、前記電解槽1で発生した水素ガスを外部に排出する排出口(図示せず)を有している。   The storage tank 6 has a discharge port (not shown) for discharging the hydrogen gas generated in the electrolytic cell 1 to the outside.

次に前記実施例1の電解装置による次亜塩素酸水の生成方法とその効果について説明する。   Next, a method for producing hypochlorous acid water by the electrolytic apparatus of Example 1 and its effect will be described.

希塩酸供給ポンプ5をその吐出流量を調整しながら駆動して希塩酸タンク3内の希塩酸を少量ずつ前記電解槽1内に底部1aから供給すると共に、前記電流量調整装置11により、前記両電極板2a,2bに通電する。   The dilute hydrochloric acid supply pump 5 is driven while adjusting its discharge flow rate to supply dilute hydrochloric acid in the dilute hydrochloric acid tank 3 little by little from the bottom 1a into the electrolytic cell 1, and the current amount adjusting device 11 allows the both electrode plates 2a to be supplied. , 2b is energized.

即ち、供給された希塩酸は前記電解槽1の下部から上部に徐々に上昇していき、この上昇中の希塩酸は前記両電極板2a、2bにより電気分解されて次亜塩素酸水を生成する。   That is, the supplied dilute hydrochloric acid gradually rises from the lower part to the upper part of the electrolytic cell 1, and the dilute hydrochloric acid in the rise is electrolyzed by the electrode plates 2a and 2b to generate hypochlorous acid water.

このとき、これら両電極板2a、2bの対向する内表面ばかりでなく外表面においても電気分解が行われるので、電気分解が効率的に行われる。また、前記電気量調整装置11により両電極板2a、2bの電流を調整して、供給される希塩酸の全部が前記混入管路9内に流入されるまでに電気分解されるようにする。   At this time, since the electrolysis is performed not only on the opposed inner surfaces of the electrode plates 2a and 2b but also on the outer surface, the electrolysis is efficiently performed. Further, the electric quantity adjusting device 11 adjusts the currents of the two electrode plates 2a and 2b so that all of the supplied dilute hydrochloric acid is electrolyzed until it flows into the mixing conduit 9.

一方、循環ポンプ8を駆動して、貯留タンク6内の水を循環管路7内を循環流動する。   On the other hand, the circulation pump 8 is driven to circulate and flow the water in the storage tank 6 through the circulation line 7.

そして、混入管路9内を流動する前記次亜塩素酸水を、混入個所Aにおいて循環管路7内を流動する水又は次亜塩素酸水に混入し、該次亜塩素酸水が貯留タンク6内に貯留されていく。   Then, the hypochlorous acid water flowing in the mixing pipe 9 is mixed into the water or hypochlorous acid water flowing in the circulation pipe 7 at the mixing point A, and the hypochlorous acid water is stored in the storage tank. 6 is stored.

初期の時点では、該貯留タンク6内の次亜塩素酸水は低濃度であるが、該次亜塩素酸水が循環管路7内の循環を繰り返しながら前記電解槽1からの次亜塩素酸水が混入されて徐々に濃度の高い次亜塩素酸水になってくる。そして貯留タンク6内の次亜塩素酸水が所望の濃度になるまで運転を継続する。   At the initial time point, the hypochlorous acid water in the storage tank 6 has a low concentration, but the hypochlorous acid from the electrolytic cell 1 is repeatedly recycled while the hypochlorous acid water repeatedly circulates in the circulation pipe 7. Water is mixed and gradually becomes hypochlorous acid water with high concentration. The operation is continued until the hypochlorous acid water in the storage tank 6 has a desired concentration.

このように、希塩酸を電解槽1内に供給ポンプ5により少量ずつ供給して、該電解槽1内で該供給された希塩酸の全部を電気分解して生成した次亜塩素酸水を循環経路7に混入する方式であるので、供給された希塩酸のうち未分解の希塩酸がなく、生成した次亜塩素酸水のpHが中性付近を示し、次亜塩素酸水の中和のためにカルシウムなどを含む硬度の高い水を必要としない。   In this way, dilute hydrochloric acid is supplied to the electrolytic cell 1 by the supply pump 5 little by little, and hypochlorous acid water generated by electrolyzing all of the supplied diluted hydrochloric acid in the electrolytic cell 1 is circulated through the circulation path 7. Since there is no undecomposed dilute hydrochloric acid among the supplied dilute hydrochloric acid, the pH of the generated hypochlorous acid water is near neutral, and calcium etc. for neutralization of hypochlorous acid water Does not require water with high hardness.

また、生成した次亜塩素酸水のpHが中性付近であるので、次亜塩素酸水を室内などに放出して室内空気を殺菌する際に、室内にある鉄やその他の金属類に対する腐食の影響を抑えることができる。   In addition, since the pH of the generated hypochlorous acid water is near neutral, when the indoor air is sterilized by releasing the hypochlorous acid water into the room, etc., corrosion to iron and other metals in the room The influence of can be suppressed.

また、生成した次亜塩素酸水のpHが中性付近であるので、次亜塩素酸水が長時間安定して、次亜塩素酸水が分解して塩素ガスが発生してしまうことを抑えることができる。   In addition, since the pH of the generated hypochlorous acid water is near neutral, the hypochlorous acid water is stable for a long time and suppresses generation of chlorine gas due to decomposition of the hypochlorous acid water. be able to.

また、該電流量調整装置11による調整電流が小電流で十分である。   Further, a small current is sufficient for the adjustment current by the current amount adjusting device 11.

また、構造がシンプルで、取り扱いが簡単であり、安全で、長期に使用でき、メンテナンスフリーな電解装置を提供することができる。   In addition, it is possible to provide an electrolyzer that has a simple structure, is easy to handle, is safe, can be used for a long time, and is maintenance-free.

なお、供給された希塩酸を電気分解すると、前記数1の反応式のように、例えば、30ppmのHClO(次亜塩素酸)に対して等量の30ppmのHCl(塩酸)が生成されるが、この程度の量の塩酸は、供給された希塩酸中に含まれるCa++、Naなどによって中和されるので、次亜塩素酸水のpHを下げるとしてもごく僅かで、生成した次亜塩素酸水のpHが中性付近から外れてしまうほどの影響はない。 In addition, when the supplied dilute hydrochloric acid is electrolyzed, for example, an equivalent amount of 30 ppm of HCl (hydrochloric acid) is generated with respect to 30 ppm of HClO (hypochlorous acid) as shown in the reaction formula 1. This amount of hydrochloric acid is neutralized by Ca ++ , Na +, etc. contained in the supplied dilute hydrochloric acid, so that even if the pH of hypochlorous acid water is lowered, the amount of generated hypochlorous acid is very small. There is no influence that the pH of water deviates from near neutrality.

なお、前記供給された希塩酸の全部が混入管路9内に流入するまでに電気分解せず、前記供給された希塩酸の一部を電気分解する場合でも、生成した次亜塩素酸水が該混入管路9内に流入される時に、該次亜塩素酸水のpHが4.0〜6.5、好ましくは5.0〜6.5の中性付近の範囲内となるように前記電流量調整装置11により前記両電極板2a,2bへの電流を調整して通電するようにしてもよい。   Even when the supplied dilute hydrochloric acid is not electrolyzed until all of the supplied dilute hydrochloric acid flows into the mixing pipe 9, and even when a part of the supplied dilute hydrochloric acid is electrolyzed, the generated hypochlorous acid water is mixed. When flowing into the pipe 9, the amount of current is adjusted so that the pH of the hypochlorous acid water is in the range of about 4.0 to 6.5, preferably about 5.0 to 6.5. The adjusting device 11 may adjust the current to both the electrode plates 2a and 2b to be energized.

前記次亜塩素酸水のpHが5.0〜6.5の中性付近の範囲内であれば、該次亜塩素酸水がもっとも安定した状態となり、次亜塩素酸水の90%以上が分解されずに維持されるので、次亜塩素酸水を殺菌水として使用した場合に、もっとも効率のよい殺菌効果を得ることができる。   If the pH of the hypochlorous acid water is within a neutral range of 5.0 to 6.5, the hypochlorous acid water is in a most stable state, and 90% or more of the hypochlorous acid water is present. Since it is maintained without being decomposed, the most efficient sterilizing effect can be obtained when hypochlorous acid water is used as sterilizing water.

本発明の次亜塩素酸水生成用電解装置の実施例2を図3により説明する。   Example 2 of the electrolyzer for generating hypochlorous acid water of the present invention will be described with reference to FIG.

この実施例2においては、実施例1の電解槽1の陽極板2a及び陰極板2bの板面に複数の貫通孔12を設ける。   In the second embodiment, a plurality of through holes 12 are provided on the plate surfaces of the anode plate 2a and the cathode plate 2b of the electrolytic cell 1 of the first embodiment.

この実施例2においては、電解槽1内の希塩酸が、該貫通孔12を通じて、両電極板2a、2bの内外表面に行き来して、両電極板の外表面も有効に電気分解に寄与することなり、従来の両電極板の内表面のみが希塩酸に接触可能な電解槽に比べて、2倍以上の電流効率を上げることができる。   In Example 2, dilute hydrochloric acid in the electrolytic cell 1 travels through the through-holes 12 to the inner and outer surfaces of both electrode plates 2a and 2b, and the outer surfaces of both electrode plates also contribute to electrolysis effectively. Thus, the current efficiency can be increased twice or more as compared with the conventional electrolytic cell in which only the inner surfaces of both electrode plates can be in contact with dilute hydrochloric acid.

なお、前記貫通孔12の形状は、例えば円形状やスリット状等のいずれの形状でもよい。   The shape of the through hole 12 may be any shape such as a circular shape or a slit shape.

また、4cm×16cm以上の大きさの電極板に貫通孔を設けるようにすれば、電流効率が特に良くなる。   Further, if the through holes are provided in the electrode plate having a size of 4 cm × 16 cm or more, the current efficiency is particularly improved.

本発明の次亜塩素酸水生成用電解装置及び次亜塩素酸水の生成方法は、食品工場、養鶏場、搾乳場、農場、医療や介護施設、レストラン等で利用される。   The electrolytic device for hypochlorous acid production and the method for producing hypochlorous acid water of the present invention are used in food factories, poultry farms, milking farms, farms, medical and nursing facilities, restaurants, and the like.

1 電解槽
2a 陽極板
2b 陰極板
3 希塩酸タンク
5 希塩酸供給ポンプ
7 循環管路
11 電流量調整装置
12 貫通孔
DESCRIPTION OF SYMBOLS 1 Electrolysis tank 2a Anode plate 2b Cathode plate 3 Dilute hydrochloric acid tank 5 Dilute hydrochloric acid supply pump 7 Circulation line 11 Current amount adjusting device 12 Through-hole

Claims (5)

下部から希塩酸が供給される電解槽と、該電解槽内に対向して設けられ対向する内表面とその反対側の外表面に希塩酸が接触可能な陽極板及び陰極板と、これら両電極板により前記下部から供給される希塩酸の全部を電気分解して次亜塩素酸水を生成し前記電解槽の上部より次亜塩素酸水が流出するように前記両電極板への電流を調整する電流量調整装置とからなる次亜塩素酸水生成用電解装置。   An electrolytic cell to which dilute hydrochloric acid is supplied from the lower part, an anode plate and a cathode plate that are provided facing the inside of the electrolyzer and are capable of contacting dilute hydrochloric acid on the opposing inner surface and the outer surface on the opposite side, The amount of current for adjusting the currents to the two electrode plates so as to electrolyze all the dilute hydrochloric acid supplied from the lower part to generate hypochlorous acid water and to flow out the hypochlorous acid water from the upper part of the electrolytic cell An electrolyzer for generating hypochlorous acid water, comprising an adjusting device. 下部から希塩酸が供給される電解槽と、該電解槽内に対向して設けられ対向する内表面とその反対側の外表面に希塩酸が接触可能な陽極板及び陰極板と、これら両電極板により前記下部から供給される希塩酸の一部を電気分解して次亜塩素酸水を生成し前記電解槽の上部より流出する該次亜塩素酸水のpHが5.0〜6.5の範囲内となるように前記両電極板への電流を調整する電流量調整装置とからなる次亜塩素酸水生成用電解装置。   An electrolytic cell to which dilute hydrochloric acid is supplied from the lower part, an anode plate and a cathode plate that are provided facing the inside of the electrolyzer and are capable of contacting dilute hydrochloric acid on the opposing inner surface and the outer surface on the opposite side, A part of dilute hydrochloric acid supplied from the lower part is electrolyzed to generate hypochlorous acid water, and the pH of the hypochlorous acid water flowing out from the upper part of the electrolytic cell is within a range of 5.0 to 6.5. An electrolyzer for generating hypochlorous acid water, comprising: a current amount adjusting device that adjusts the current to both the electrode plates so that 前記陽極板及び陰極板の板面にそれぞれ複数の貫通孔を形成した請求項1又は請求項2に記載の次亜塩素酸水生成用電解装置。   The electrolytic device for hypochlorous acid water generation according to claim 1 or 2, wherein a plurality of through holes are formed on the plate surfaces of the anode plate and the cathode plate, respectively. 対向する内表面とその反対側の外表面において電気分解可能な陽極板及び陰極板を有する電解槽に希塩酸を該電解槽の下部より供給し、該電解槽内に供給される希塩酸の全部を電気分解して次亜塩素酸水を生成し、前記両電極板への電流を調整して前記電解槽の上部から次亜塩素酸水を流出するようにした次亜塩素酸水の生成方法。   Dilute hydrochloric acid is supplied from the lower part of the electrolytic cell to an electrolytic cell having an anode plate and a cathode plate that can be electrolyzed on the opposite inner surface and the outer surface on the opposite side, and all of the diluted hydrochloric acid supplied into the electrolytic cell is electrically A method for generating hypochlorous acid water, wherein hypochlorous acid water is generated by decomposition and the current to both electrode plates is adjusted to flow out the hypochlorous acid water from the upper part of the electrolytic cell. 対向する内表面とその反対側の外表面において電気分解可能な陽極板及び陰極板を有する電解槽に希塩酸を該電解槽の下部より供給し、該電解槽内に供給される希塩酸の一部を電気分解して次亜塩素酸水を生成し、前記両電極板への電流を調整して前記電解槽の上部からpHが5.0〜6.5の範囲内の次亜塩素酸水を流出するようにした次亜塩素酸水の生成方法。   Dilute hydrochloric acid is supplied from the lower part of the electrolytic cell to an electrolytic cell having an anode plate and a cathode plate that can be electrolyzed on the opposing inner surface and the opposite outer surface, and a part of the diluted hydrochloric acid supplied into the electrolytic cell is supplied to the electrolytic cell. Electrolyze to produce hypochlorous acid water, adjust the current to both electrode plates, and flow out hypochlorous acid water in the range of pH 5.0 to 6.5 from the upper part of the electrolytic cell A method for producing hypochlorous acid water.
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