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 PDFInfo
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 80
- QWPPOHNGKGFGJK-UHFFFAOYSA-N hypochlorous acid Chemical compound ClO QWPPOHNGKGFGJK-UHFFFAOYSA-N 0.000 title claims abstract description 73
- 238000000034 method Methods 0.000 title claims abstract description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 61
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 238000000354 decomposition reaction Methods 0.000 claims description 2
- 230000001954 sterilising effect Effects 0.000 abstract description 4
- 238000004659 sterilization and disinfection Methods 0.000 abstract 1
- 238000005868 electrolysis reaction Methods 0.000 description 6
- 239000011575 calcium Substances 0.000 description 4
- 230000007935 neutral effect Effects 0.000 description 4
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000000474 nursing effect Effects 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
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Abstract
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).
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,
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
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。
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。
10は貯留タンク6の排出管を示す。
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
(数1)
2HCl+H2O→HCl+HClO+H2
(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
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
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
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
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
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
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
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
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
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
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
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
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
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
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JP2015147197A (en) * | 2014-02-07 | 2015-08-20 | パナソニックIpマネジメント株式会社 | Annihilation device for microbe in ballast water |
WO2017064577A1 (en) * | 2015-08-25 | 2017-04-20 | Bar-Ilan University | Asymmetric electrochemical cell apparatus, and operating methods thereof |
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