JP2009136814A - Preparation method of weak acidic electrolytic water - Google Patents

Preparation method of weak acidic electrolytic water Download PDF

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JP2009136814A
JP2009136814A JP2007317785A JP2007317785A JP2009136814A JP 2009136814 A JP2009136814 A JP 2009136814A JP 2007317785 A JP2007317785 A JP 2007317785A JP 2007317785 A JP2007317785 A JP 2007317785A JP 2009136814 A JP2009136814 A JP 2009136814A
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hydrochloric acid
water
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sodium bicarbonate
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JP2009136814A5 (en
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Toyohiko Doi
土井豊彦
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<P>PROBLEM TO BE SOLVED: To provide a method for preparing weak acidic electrolytic water with a predetermined pH even when low hardness water is used without requiring labor for adjusting an electrolytic condition and lowering the occurrence efficiency of elemental chlorine by solving the problem that pH is lowered according to circumstances if raw water extremely low in hardness is used in a method for preparing weak acidic electrolytic water by electrolyzing dilute hydrochloric acid in a non-diaphragm electrolytic cell and the adjustment of the electrolytic condition or the adjustment for lowering the concentration of the raw material hydrochloric acid is required. <P>SOLUTION: By substituting a part of hydrogen ions with sodium ions by dissolving sodium bicarbonate in the diluting water of hydrochloric acid, even when water low in hardness is used, weak acidic electrolytic water with proper pH can be prepared without requiring the fine adjustment of the electrolytic condition or operation for lowering electrolytic efficiency such as the concentration lowering operation of hydrochloric acid or the like. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は希塩酸を電気分解し、水で希釈して微酸性電解水を調製する技術に関する。より詳しくは、電気分解して微酸性電解水を調製する原料の希塩酸を調製する技術に関する。 The present invention relates to a technique for preparing slightly acidic electrolyzed water by electrolyzing dilute hydrochloric acid and diluting it with water. More specifically, the present invention relates to a technique for preparing dilute hydrochloric acid as a raw material for electrolyzing to prepare slightly acidic electrolyzed water.

近年の衛生医療分野は、人の移動の激化や、食品や食品材料流通のグローバル化あるいは抗生剤に頼る医療などに見られる社会的変化に伴って、耳慣れない病原体や薬剤耐性の微生物によって引き起こされる大規模感染や難治癒疾病に直面している。それらのニュースに日々接している国民の不安は募り、いきおい衛生対策に対する関心も高まっている。それに伴って、対策としての殺菌剤、殺菌機能付商品の市場は拡大を続けている。そのような中、10数年前に殺菌剤の新顔として登場した、塩素イオンの電解により生成される所謂殺菌用電解水は、厚労省の規格制定などの後押しもあり、国民生活の中に定着しつつある。 In recent years, the field of hygiene and medical care is caused by pathogens and drug-resistant microorganisms that are unfamiliar to ears, due to intensifying human movement, globalization of the distribution of food and food materials, and social changes such as medical care that relies on antibiotics. Facing outbreaks and incurable diseases. The people who are in contact with these news every day are worried and the interest in hygiene measures is growing. Along with this, the market for bactericides as a countermeasure and products with bactericidal functions continues to expand. Under such circumstances, so-called bactericidal electrolyzed water produced by electrolysis of chloride ions, which appeared as a new face of bactericides 10 years ago, has been supported by the establishment of the Ministry of Health, Labor and Welfare standards, Is becoming established.

殺菌用電解水の中の微酸性電解水(食品添加物名「微酸性次亜塩素酸水」)は希塩酸を無隔膜電解槽で電気分解して生成される(特許文献1)。したがって、塩類を殆んど含まず、周囲への影響もないため、通常の殺菌洗浄としての利用法の他、噴霧使用が可能で、環境殺菌、脱臭、安全な加湿など幅広い利用が始まっている。本発明はこの微酸性電解水の生成における便宜性をさらに高め、普及に拍車をかける目的で行われたものである。
特許第3798486号
Slightly acidic electrolyzed water (name of food additive “slightly acidic hypochlorous acid water”) in the sterilized electrolyzed water is generated by electrolyzing dilute hydrochloric acid in a non-diaphragm electrolyzer (Patent Document 1). Therefore, it contains almost no salt and has no effect on the surroundings, so it can be used for spraying in addition to the usual use for sterilization and washing, and has started to be widely used for environmental sterilization, deodorization, safe humidification, etc. . The present invention was carried out for the purpose of further enhancing convenience in the production of the slightly acidic electrolyzed water and spurring its popularization.
Japanese Patent No. 3798486

前述のように多くの優れた性質を持った微酸性電解水は徐々に普及しているが、さらに普及を促進するためにはその生成方法において利便性を高めることが求められている。 As described above, slightly acidic electrolyzed water having many excellent properties is gradually spreading, but in order to further promote the spread, it is required to improve convenience in its production method.

微酸性電解水は希塩酸を無隔膜電解槽で電解し、生成した電解液を水で希釈することによって調製される。希塩酸に含まれる塩素イオンが化1式のように電極酸化されて単体の塩素となり、その塩素が水と反応して化2式のように次亜塩素酸(HOCl)が生成される。 The slightly acidic electrolyzed water is prepared by electrolyzing dilute hydrochloric acid in a non-diaphragm electrolyzer and diluting the produced electrolyte with water. Chlorine ions contained in dilute hydrochloric acid are electrode oxidized as shown in chemical formula 1 to form single chlorine, and the chlorine reacts with water to generate hypochlorous acid (HOCl) as shown in chemical formula 2.

(化1) 2HCl → H2
+ Cl2
(Chemical formula 1) 2HCl → H 2
+ Cl 2

(化2) Cl2
+ H2O → HOCl + HCl
(Chemical formula 2 ) Cl 2
+ H 2 O → HOCl + HCl

この次亜塩素酸が殺菌成分である。ところが、化2式から分かるように次亜塩素酸と同時に塩酸が発生する。このようにして発生した塩酸の一部はそのまま電解槽から排出されることがある。電解槽を出た後水により希釈されるが、希釈倍率が1000倍以上と極めて高いために、通常は、希釈の効果と希釈水に含まれる硬度成分によって中和され、生成水は名前の通り微酸性領域のpHを示すことになる。 This hypochlorous acid is a bactericidal component. However, as can be seen from the chemical formula 2, hydrochloric acid is generated simultaneously with hypochlorous acid. Part of the hydrochloric acid generated in this way may be discharged from the electrolytic cell as it is. After leaving the electrolytic cell, it is diluted with water, but since the dilution ratio is extremely high, 1000 times or more, it is usually neutralized by the effect of dilution and the hardness component contained in the diluted water, and the generated water is as the name suggests. It indicates the pH of the slightly acidic region.

しかし、希釈水の硬度が極めて低い場合は、硬度成分による中和作用が低いため、所定のpHを下回ることもあり、その対策として電解条件を調整し、電解槽から排出される塩酸量を減少させる必要があった。又他の対策として、元々の希塩酸の濃度を低くしておくという方法もある。しかし、原料の塩酸の濃度が低くなれば、当然塩素イオン濃度が低下し、電解時の単体塩素の発生効率も低下してしまう。そこで、本発明者は、希塩酸を無隔膜電解槽で電解し微酸性電解水を生成する方法において、電解条件を調整する手間を要せず、かつ単体塩素の発生効率を低下させず、低硬度水を使用したときにも所定のpHの微酸性電解水を調製する方法を提供することを課題とした。 However, when the hardness of the dilution water is extremely low, the neutralization effect by the hardness component is low, so it may be lower than the predetermined pH. As a countermeasure, the electrolysis conditions are adjusted and the amount of hydrochloric acid discharged from the electrolytic cell is reduced. It was necessary to let them. As another countermeasure, there is a method of reducing the original concentration of dilute hydrochloric acid. However, if the concentration of the hydrochloric acid as the raw material is lowered, the chlorine ion concentration is naturally lowered, and the generation efficiency of simple chlorine during electrolysis is also lowered. Therefore, the present inventor, in a method for producing slightly acidic electrolyzed water by electrolyzing dilute hydrochloric acid in a diaphragmless electrolytic cell, does not require time and effort to adjust electrolysis conditions, does not reduce the generation efficiency of simple chlorine, and has low hardness. An object of the present invention is to provide a method for preparing slightly acidic electrolyzed water having a predetermined pH even when water is used.

多くの優れた性質を持った微酸性電解の普及を促進するためにはその生成方法において利便性を高めることが必要であり、そのために、本発明者は電解条件を調整せず、かつ単体塩素の発生効率の低下も伴わず、低硬度水を使用したときにも所定のpHの微酸性電解水を調製する方法を提供するための手段の研究を進めた。 In order to promote the spread of slightly acidic electrolysis having many excellent properties, it is necessary to improve convenience in its production method. For this reason, the present inventor did not adjust the electrolysis conditions and used simple chlorine. The research on means for providing a method for preparing slightly acidic electrolyzed water having a predetermined pH even when low-hardness water is used has been advanced.

そこでまず、化1式と化2式をそれぞれの辺どうし足し合わせ整理すると、化3式に示した電解反応全体を通した物質の収支式が得られることに着目した。 First, attention was paid to the fact that the balance equation of the substance through the entire electrolytic reaction shown in the chemical formula 3 can be obtained by adding and organizing the chemical formula 1 and the chemical formula 2 together.

(化3) 2H+
+ 2Cl- + H2O → H2 + HOCl
この化3式は、最初の塩酸が解離して生成した水素イオンが水素ガスとなって系外に出ることによりpHが上昇することを示している。従って、電解液中の塩酸残量を少なくするための他の方法として考えられるのは、電解前の水素イオン濃度を下げておけばよいと考えた。さらに、原液の塩素イオン濃度を下げず、かつ原液の電気伝導度を下げない方法としては、水素イオンの一部を、他の陽イオンで置き換えておけばよいということに着想した。
(Chemical 3) 2H +
+ 2Cl - + H 2 O → H 2 + HOCl
This chemical formula 3 shows that the pH is increased by hydrogen ions generated by dissociation of the first hydrochloric acid as hydrogen gas and out of the system. Therefore, as another method for reducing the remaining amount of hydrochloric acid in the electrolytic solution, it was considered that the hydrogen ion concentration before electrolysis should be lowered. Furthermore, as a method for reducing the chlorine ion concentration of the stock solution and not lowering the electrical conductivity of the stock solution, the inventors conceived that some of the hydrogen ions may be replaced with other cations.

そして、本発明者は、塩酸を希釈する水に重炭酸ナトリウムを溶解しておくことで、化4式に示すような反応によって、水素イオンの一部がナトリウムイオンによって置換され、その他の化学成分が塩酸のみを水で希釈したときと同じであることを確認して、これを、課題を解決するための第1の態様とした。 Then, the present inventor dissolved sodium bicarbonate in water for diluting hydrochloric acid, whereby a part of hydrogen ions was replaced by sodium ions by the reaction shown in the chemical formula 4, and other chemical components Was the same as when only hydrochloric acid was diluted with water, and this was made the first mode for solving the problem.

(化4) NaHCO3
+ Cl- + H+ → Na+ + Cl-
+H2O + CO
(Chemical Formula 4) NaHCO 3
+ Cl - + H + → Na + + Cl -
+ H 2 O + CO 2

次に、重炭酸ナトリウムの添加量については、原水の硬度に応じて増減する必要があると考えられるが、日本国内の水道水について硬度の調査をした結果、公共水道として最も低硬度と考えられるのが10ppm前後であった。そこで、希塩酸の塩酸濃度を20%以下とするとき、硬度10ppmの水で所定のpH の微酸性電解水を調製することができる塩酸希釈水の重炭酸ナトリウム濃度が700ppmであることを確認し、又、硬度40ppmの水で所定のpH の微酸性電解水を調製することができる塩酸希釈水の重炭酸ナトリウム濃度が300ppmであることも確認するに至り、希釈水の重炭酸ナトリム濃度を0.1ppm以上、700ppm以下、より好ましくは300ppm以上、700ppm以下とすることを、課題を解決するための第2の態様とした。 Next, the amount of sodium bicarbonate added may need to be increased or decreased depending on the hardness of the raw water, but as a result of a survey of the hardness of tap water in Japan, it is considered to have the lowest hardness for public water supply. Was around 10 ppm. Accordingly, when the hydrochloric acid concentration of dilute hydrochloric acid is 20% or less, it is confirmed that the sodium bicarbonate concentration of hydrochloric acid-diluted water capable of preparing a slightly acidic electrolyzed water having a predetermined pH with water having a hardness of 10 ppm is 700 ppm. It has also been confirmed that the sodium bicarbonate concentration of hydrochloric acid-diluted water in which slightly acidic electrolyzed water having a predetermined pH can be prepared with water having a hardness of 40 ppm is 300 ppm. The second mode for solving the problem is to set 1 ppm to 700 ppm, more preferably 300 ppm to 700 ppm.

さらに以上のような重炭酸ナトリウム溶液で予め希釈調製した希塩酸は、そのまま軟水を原料とする微酸性電解水の調製に利用できることに着想し、重炭酸ナトリム濃度が0.1ppm以上、700ppm以下、より好ましくは300ppm以上、700ppm以下の重炭酸ナトリウム溶液で希釈調製した希塩酸を課題を解決するための第3の態様としたことにより、本発明を完成させた。 Furthermore, the dilute hydrochloric acid prepared by diluting in advance with the sodium bicarbonate solution as described above can be used as it is for the preparation of slightly acidic electrolyzed water using soft water as a raw material, and the sodium bicarbonate concentration is 0.1 ppm or more and 700 ppm or less. The present invention was completed by using diluted hydrochloric acid diluted with a sodium bicarbonate solution of preferably 300 ppm or more and 700 ppm or less as a third embodiment for solving the problems.

本発明によって、塩酸を希釈する水に重炭酸ナトリウムを溶解しておくことで、硬度の極端に低い原水を使って微酸性電解水を調製するときにも、電解条件の調整や希塩酸濃度を下げるなどの対策をしないでも所定pHの微酸性電解水を調製することができるようになった。 By dissolving sodium bicarbonate in water for diluting hydrochloric acid according to the present invention, even when preparing slightly acidic electrolyzed water using raw water with extremely low hardness, adjustment of electrolysis conditions and dilute hydrochloric acid concentration are reduced. It is now possible to prepare slightly acidic electrolyzed water having a predetermined pH without taking measures such as the above.

あるいはまた、本発明によれば、希釈水の重炭酸ナトリム濃度を0.1ppm以上、700ppm以下、より好ましくは300ppm以上、700ppm以下とすることによって、硬度が10ppm程度の原水でも適正なpHの微酸性電解水を生成することができるようになった。さらには、重炭酸ナトリム濃度が0.1ppm以上、700ppm以下、より好ましくは300ppm以上、700ppm以下の重炭酸ナトリウム溶液で希釈調製した希塩酸を提供することにより、軟水でも手軽に適正pH の微酸性電解水を精製することが可能になった。 Alternatively, according to the present invention, the concentration of sodium bicarbonate in diluted water is 0.1 ppm or more and 700 ppm or less, more preferably 300 ppm or more and 700 ppm or less. Acidic electrolyzed water can be generated. Further, by providing dilute hydrochloric acid diluted with a sodium bicarbonate solution having a sodium bicarbonate concentration of 0.1 ppm or more and 700 ppm or less, more preferably 300 ppm or more and 700 ppm or less, a slight acidic electrolysis with an appropriate pH can be easily performed even in soft water. It became possible to purify the water.

次に、本発明の理解を確実にするために実施例を元に本発明を実施するための最良の形態の一例を説明する。但し、実施例の記載内容は各実施例に限定されるもので、本特許の請求範囲とは直接の関係は無い。 Next, in order to ensure an understanding of the present invention, an example of the best mode for carrying out the present invention will be described based on the examples. However, the description of the examples is limited to each example, and is not directly related to the claims of this patent.

35%濃度の食品添加物塩酸を、700ppmの重炭酸ナトリウム溶液で希釈し、9%の希塩酸を調製した。この希塩酸を使い、図1にフロー図を示した自作の電解装置を使って微酸性電解水を生成した。電解槽(2)は10×20cmの平板電極で3セルの複極式とした。カルシウム硬度10ppmの原水は定流量弁(3)によって300L/hの一定流量に調整し、電解電圧は2.5Vの定電圧、電解電流は目標30Aとした。希塩酸は、電流値が30Aを切ったとき希塩酸供給ポンプ(1)で電解槽に供給し、30Aを超えたときに供給を停止するように制御し生成した。その結果、有効塩素濃度18ppm、pH5.6の微酸性電解水が300L/hで生成された。 35% strength food additive hydrochloric acid was diluted with 700 ppm sodium bicarbonate solution to prepare 9% dilute hydrochloric acid. Using this dilute hydrochloric acid, slightly acidic electrolyzed water was produced using a self-made electrolyzer whose flow diagram is shown in FIG. The electrolytic cell (2) was a 10 × 20 cm plate electrode and a 3 cell bipolar type. The raw water with a calcium hardness of 10 ppm was adjusted to a constant flow rate of 300 L / h by a constant flow valve (3), the electrolysis voltage was a constant voltage of 2.5 V, and the electrolysis current was a target of 30 A. The dilute hydrochloric acid was generated by supplying the dilute hydrochloric acid supply pump (1) to the electrolytic cell when the current value cuts off 30A, and stopping the supply when the current value exceeded 30A. As a result, slightly acidic electrolyzed water having an effective chlorine concentration of 18 ppm and a pH of 5.6 was produced at 300 L / h.

また別の実施例で本発明を実施するための別の最良の形態の一例を説明する。35%濃度の食品添加物塩酸を、300ppmの重炭酸ナトリウム溶液で希釈し、9%の希塩酸を調製した。この希塩酸を使い、実施例1と同じ装置を使って微酸性電解水を生成した。カルシウム硬度40ppmの原水流量を300L/hとし、電解電圧2.5V、電解電流30Aで生成した結果、有効塩素濃度20ppm、pH5.8の微酸性電解水が300L/hで生成された。 Another example of another best mode for carrying out the present invention will be described in another example. 35% strength food additive hydrochloric acid was diluted with 300 ppm sodium bicarbonate solution to prepare 9% dilute hydrochloric acid. Using this dilute hydrochloric acid, slightly acidic electrolyzed water was produced using the same apparatus as in Example 1. The raw water flow rate with a calcium hardness of 40 ppm was 300 L / h, and the electrolysis voltage was 2.5 V and the electrolysis current was 30 A. As a result, slightly acidic electrolyzed water having an effective chlorine concentration of 20 ppm and a pH of 5.8 was produced at 300 L / h.

さらに別の実施例で本発明を実施するための又別の最良の形態の一例を説明する。35%濃度の食品添加物塩酸を、700ppmの重炭酸ナトリウム溶液で希釈し、9%の希塩酸を調製した。この希塩酸を使い、実施例1と同じ装置を使って微酸性電解水を生成した。カルシウム硬度110ppmの原水流量を300L/hとし、電解電圧2.2V、電解電流30Aで生成した結果、有効塩素濃度20ppm、pH6.0の微酸性電解水が300L/hで生成された。 Further, another example of another best mode for carrying out the present invention will be described. 35% strength food additive hydrochloric acid was diluted with 700 ppm sodium bicarbonate solution to prepare 9% dilute hydrochloric acid. Using this dilute hydrochloric acid, slightly acidic electrolyzed water was produced using the same apparatus as in Example 1. The raw water flow rate with a calcium hardness of 110 ppm was 300 L / h, and the electrolysis voltage was 2.2 V and the electrolysis current was 30 A. As a result, slightly acidic electrolyzed water having an effective chlorine concentration of 20 ppm and a pH of 6.0 was produced at 300 L / h.

実施例説明のための微酸性電解水生成装置フロー図Flowchart of slightly acidic electrolyzed water generating apparatus for explaining examples

符号の説明Explanation of symbols

1 希塩酸供給ポンプ
2 電解槽
3 定流量弁
4 直流定電圧電源
5 制御装置
6 希塩酸タンク
DESCRIPTION OF SYMBOLS 1 Dilute hydrochloric acid supply pump 2 Electrolyzer 3 Constant flow valve 4 DC constant voltage power supply 5 Control apparatus 6 Dilute hydrochloric acid tank

Claims (3)

希塩酸を無隔膜電解槽で電気分解し、水で希釈することによって微酸性電解水を生成する方法において、用いる希塩酸が、塩酸を、重炭酸ナトリウム溶液で希釈調製したものであることを特徴とする微酸性電解水の生成法 In a method for producing slightly acidic electrolyzed water by electrolyzing dilute hydrochloric acid in a diaphragmless electrolytic cell and diluting with water, dilute hydrochloric acid to be used is prepared by diluting hydrochloric acid with sodium bicarbonate solution. Generation method of slightly acidic electrolyzed water 塩酸の希釈に用いる重炭酸ナトリウム溶液の重炭酸ナトリウムの濃度が0.1ppm以上、700ppm以下、より好ましくは300ppm以上、700ppm以下であることを特徴とする請求項1記載の微酸性電解水の生成法 2. The slightly acidic electrolyzed water according to claim 1, wherein the concentration of sodium bicarbonate in the sodium bicarbonate solution used for diluting hydrochloric acid is 0.1 ppm or more and 700 ppm or less, more preferably 300 ppm or more and 700 ppm or less. Law 重炭酸ナトリウム溶液、より好ましくは0.1ppm以上、700ppm以下、さらに好ましくは300ppm以上、700ppm以下の重炭酸ナトリウム溶液、で希釈調製された希塩酸
Dilute hydrochloric acid diluted with a sodium bicarbonate solution, more preferably 0.1 ppm to 700 ppm, and even more preferably 300 ppm to 700 ppm sodium bicarbonate solution
JP2007317785A 2007-12-08 2007-12-08 Preparation method of weak acidic electrolytic water Pending JP2009136814A (en)

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Cited By (7)

* Cited by examiner, † Cited by third party
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KR100970708B1 (en) * 2009-09-01 2010-07-16 한국코스믹라운드(주) Method and apparatus for producing slight acidic hypochlorous acid water
JP2011088149A (en) * 2011-02-07 2011-05-06 Bisansei Denkaisui Kenkyusho:Kk Method of preparing electrolyzed water and composition
CN102205294A (en) * 2010-03-31 2011-10-05 株式会社微酸性电解水研究所 Liquid spraying method and device
WO2013047922A1 (en) * 2011-09-28 2013-04-04 동인메디텍 주식회사 Apparatus for manufacturing a non-acidic hypochlorous acid solution
CN104710056A (en) * 2015-04-02 2015-06-17 金刚宝石水高科技有限公司 System and method for producing electrolytic treatment solutions
US20150189889A1 (en) * 2012-06-28 2015-07-09 Molex Incorporated Acidic electrolyzed water, and manufacturing method for same
CN115874198A (en) * 2023-02-09 2023-03-31 聊城颐鲁新材料有限公司 Method for producing subacid hypochlorous acid water without adding hydrochloric acid for diaphragm-free electrolytic cell

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KR100970708B1 (en) * 2009-09-01 2010-07-16 한국코스믹라운드(주) Method and apparatus for producing slight acidic hypochlorous acid water
CN102205294A (en) * 2010-03-31 2011-10-05 株式会社微酸性电解水研究所 Liquid spraying method and device
JP2011088149A (en) * 2011-02-07 2011-05-06 Bisansei Denkaisui Kenkyusho:Kk Method of preparing electrolyzed water and composition
WO2013047922A1 (en) * 2011-09-28 2013-04-04 동인메디텍 주식회사 Apparatus for manufacturing a non-acidic hypochlorous acid solution
US20150189889A1 (en) * 2012-06-28 2015-07-09 Molex Incorporated Acidic electrolyzed water, and manufacturing method for same
US10080367B2 (en) 2012-06-28 2018-09-25 Molex, Llc Acidic electrolyzed water and production method therefor
CN108640231A (en) * 2012-06-28 2018-10-12 莫列斯公司 Acidic electrolytic water and preparation method thereof
CN104710056A (en) * 2015-04-02 2015-06-17 金刚宝石水高科技有限公司 System and method for producing electrolytic treatment solutions
CN115874198A (en) * 2023-02-09 2023-03-31 聊城颐鲁新材料有限公司 Method for producing subacid hypochlorous acid water without adding hydrochloric acid for diaphragm-free electrolytic cell

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