JPH11192485A - Production of free hydroxide ion - Google Patents

Production of free hydroxide ion

Info

Publication number
JPH11192485A
JPH11192485A JP36817197A JP36817197A JPH11192485A JP H11192485 A JPH11192485 A JP H11192485A JP 36817197 A JP36817197 A JP 36817197A JP 36817197 A JP36817197 A JP 36817197A JP H11192485 A JPH11192485 A JP H11192485A
Authority
JP
Japan
Prior art keywords
cathode
ions
anode
free hydroxyl
electrolyte
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP36817197A
Other languages
Japanese (ja)
Inventor
Yukiaki Matsuo
尾 至 明 松
Kokichi Hanaoka
岡 孝 吉 花
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
RIVER SUTON KK
Original Assignee
RIVER SUTON KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by RIVER SUTON KK filed Critical RIVER SUTON KK
Priority to JP36817197A priority Critical patent/JPH11192485A/en
Publication of JPH11192485A publication Critical patent/JPH11192485A/en
Pending legal-status Critical Current

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  • Water Treatment By Electricity Or Magnetism (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PROBLEM TO BE SOLVED: To stably produce free hydroxide ion water containing free hydroxide ion by electrolyzing an electrolytic solution in an electrolyzer to form free hydroxide ions on the cathode side, and collecting the electrolytically produced liquid from the electrolyzer to remove the electrolyte by a distillation method, a reverse osmosis method, or the like. SOLUTION: The electrolytically formed produced liquid containing free ion seeds is electrolized by using an electrolyzer 1. That is, an electrolytic solution 6 is allowed to flow into the electrolyzer 1 from an inflow port 6a, and it is passed between a cathode 2, an anode 3, and a diaphragm 4 to allow it to flow out as produced liquids 7, 8 on the cathode and anode sides from outflow ports 7a, 7b on the cathode and anode sides, respectively. The cathode 2 and the anode 3 each consist of inert electrodes, and as the inert electrodes, platinum electrodes are used, and as an electrolytic aid of the electrolytic solution 6, sodium chloride is used. An electric current is applied to between both the electrodes 2, 3 from DC power supply 5 to electrolytically form free ions on both the electrodes 2, 3. The electrolytically produced liquid 7 is distilled by a distillation device 9 to form free hydroxide ion water 10 from which electrolyte has been removed.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は陰極と陽極を具備し
た電解槽内に電解質溶液を入れ、その両極間に直流電圧
を印加し電解する電解装置を用いた遊離イオンを含有し
た電解生成液中の遊離イオンの製造法に関し、更に詳細
には陰極側に遊離水酸イオンを、陽極側に遊離水素イオ
ンを集めるようにした電解生成液中の遊離イオンの製造
法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrolysis solution containing free ions using an electrolysis apparatus in which an electrolytic solution is placed in an electrolytic cell having a cathode and an anode, and a direct current voltage is applied between the two electrodes to perform electrolysis. More particularly, the present invention relates to a method for producing free ions in an electrolytic solution in which free hydroxyl ions are collected on the cathode side and free hydrogen ions are collected on the anode side.

【0002】[0002]

【従来の技術】従来、水の電気分解は電解助剤として塩
化ナトリウムや塩化カリウムのような電解質を用いて行
なわれてきた。また硫酸のように実際は反応に関与しな
い支持電解質を用い水の電気分解も行なわれてきた。前
者のようにハロゲン化物を用いた場合は、十分なイオン
解離が行なわれるため、電解質は完全に電離している。
そのため電解液中では、陰イオンは陽極に、陽イオンは
陰極に拡散移動し、溶液中での電荷を帯びたイオンが移
動する役割を果たす。従って陽極では、ハロゲン元素、
例えば塩素イオンが電子を放出して塩素原子から塩素分
子になる。また水分子が陽極で電子を放出し水素イオン
と酸素分子を生成し、陰極から拡散移動してきた塩素イ
オンと反応して塩酸ができる。塩酸ができると水素イオ
ン濃度が低くなり塩素ガスは一部次亜塩素酸になる。陽
極側では塩酸と次亜塩素酸により酸性溶液となり、塩素
ガスと酸素ガスは一定分圧下において気液平衡が維持さ
れている。
2. Description of the Related Art Conventionally, electrolysis of water has been carried out using an electrolyte such as sodium chloride or potassium chloride as an electrolysis aid. Also, electrolysis of water has been performed using a supporting electrolyte that does not actually participate in the reaction, such as sulfuric acid. When a halide is used as in the former case, sufficient ion dissociation is performed, and the electrolyte is completely ionized.
Therefore, in the electrolytic solution, the anions diffuse and move to the anode and the cations diffuse to the cathode, and the charged ions in the solution play a role of moving. Therefore, at the anode, the halogen element,
For example, chlorine ions emit electrons to convert chlorine atoms into chlorine molecules. In addition, water molecules emit electrons at the anode to generate hydrogen ions and oxygen molecules, and react with chlorine ions diffused and moved from the cathode to form hydrochloric acid. When hydrochloric acid is formed, the hydrogen ion concentration decreases, and chlorine gas partially becomes hypochlorous acid. On the anode side, hydrochloric acid and hypochlorous acid form an acidic solution, and the gas-liquid equilibrium is maintained between chlorine gas and oxygen gas under a constant partial pressure.

【0003】一方、陰極では電解質であるアルカリ金
属、例えばナトリウムイオンと水酸イオンとで水酸化ナ
トリウムが生成され、水の電解により水素ガスが生成さ
れる。従って、陰極側では水酸化ナトリウムによりアル
カリ性を示す結果となる。以上の結果、陽極側では酸性
を示し、陰極側ではアルカリ性を示すことになる。ま
た、それら陰極と陽極の間に配置した隔膜として荷電膜
を用いた場合、例えば陽イオン交換膜の場合は、電解質
溶液中の陽イオンのみが陽極側から陰極側に移動し、陰
イオン交換膜の場合は、電解質溶液中の陰イオンのみが
陰極側から陽極側に移動する。
On the other hand, at the cathode, sodium hydroxide is generated by an alkali metal, for example, sodium ion and hydroxide ion, which are electrolytes, and hydrogen gas is generated by electrolysis of water. Therefore, on the cathode side, the result shows alkalinity by sodium hydroxide. As a result, the anode side shows acidity and the cathode side shows alkalinity. Further, when a charged membrane is used as a diaphragm disposed between the cathode and the anode, for example, in the case of a cation exchange membrane, only cations in the electrolyte solution move from the anode side to the cathode side, and the anion exchange membrane In this case, only the anions in the electrolyte solution move from the cathode side to the anode side.

【0004】陰極と陽極間に直流印加電流を流して電解
し生成した電解生成液の生体への利用は既に古くから知
られており、電解質として塩化ナトリウムを用いた場
合、陽極で生成される次亜塩素酸が強力な殺菌作用を具
備しているということから消毒剤の代わりに使用されて
いる。また前記した電解において、硫酸根が存在する場
合、陽極側にヒドロキシラジカルが生成されることも既
に知られており、生体に直接使用した場合、生体の生体
防御機構になんらかの影響を与えることにより、免疫機
能を高めているという説もある。
[0004] The use of an electrolyzed product formed by electrolysis by applying a direct current between a cathode and an anode to a living body has been known for a long time. When sodium chloride is used as an electrolyte, the following solution is generated at the anode. Chlorous acid is used instead of a disinfectant because of its strong bactericidal action. In addition, in the above-described electrolysis, it is already known that when a sulfate group is present, a hydroxyl radical is generated on the anode side, and when used directly on a living body, by exerting some influence on a biological defense mechanism of the living body, Some say that it enhances immune function.

【0005】一方、陰極側における利用としては、水道
水を電解し、陰極側に生成される電解水を飲用すること
で、胃腸内の異常発酵を抑制したり、胃酸の抑制をする
ことができるということで、広く利用されている。陰極
側で生成されるアルカリ性の電解水は、アルカリ金属の
水酸化物であり、特にカルシウムの場合、水酸化カルシ
ウムとして水に溶解している。また、陰極表面で、水分
子が還元され、水素ガスが生成されている。陰極側生成
電解水では水素ガスを多く含むため、水との濃度比から
酸化還元電位が低くなり、−300mVにも達すること
がある。これらの利用目的のために電解装置は水道直結
式となり、簡単な操作で陰極側と陽極側の両方から電解
生成液を採取することができる。また電解生成された液
の特性を示すために溶液の酸化還元電位と水素イオン濃
度が指標として利用されている。
On the other hand, as for use on the cathode side, it is possible to suppress abnormal fermentation in the gastrointestinal tract and suppress gastric acid by electrolyzing tap water and drinking the electrolytic water generated on the cathode side. Therefore, it is widely used. The alkaline electrolyzed water generated on the cathode side is a hydroxide of an alkali metal, and particularly in the case of calcium, is dissolved in water as calcium hydroxide. Further, water molecules are reduced on the cathode surface, and hydrogen gas is generated. Since the cathode-side generated electrolyzed water contains a large amount of hydrogen gas, the oxidation-reduction potential is lowered due to the concentration ratio with water, and may reach as high as -300 mV. For these purposes, the electrolyzer is directly connected to the water supply, and the electrolysis product can be collected from both the cathode side and the anode side by a simple operation. The oxidation-reduction potential of the solution and the hydrogen ion concentration are used as indices to indicate the characteristics of the electrolytically generated solution.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、前記し
た陰極側電解生成液ではアルカリ金属の水酸化物と水素
ガスが組成として知られており、前記したように指標と
しては酸化還元電位と水素イオン濃度が採用されてい
る。陰極側電解生成液においては還元性の指標として酸
化還元電位を用いているが、該液における酸化還元電位
はネルンストの式により水素ガスと水との濃度相関及び
水素イオン濃度により決定されており、必ずしも還元性
の指標になり得ていない。さらに水酸化物と水素ガスに
よりフリーラジカルであるスーパーオキサイドアニオン
ラジカルを消去する作用を持つスカーベンジャーにはな
り得ない。同様に陽極側電解生成液においては塩酸のよ
うな酸と酸素ガスと次亜塩素酸が組成として知られてい
るが、殺菌消毒作用としては次亜塩素酸がその役割を担
っていることは自明である。しかし、肉芽形成促進等の
現象はこれらの組成では説明がしにくく、治癒系に対す
る独立した系の存在を見いださなくてはならない。
However, in the above-mentioned cathodic electrolysis solution, alkali metal hydroxide and hydrogen gas are known as compositions, and as described above, the indicators are the oxidation-reduction potential and the hydrogen ion concentration. Has been adopted. In the cathodic electrolysis solution, the oxidation-reduction potential is used as an index of reducibility, but the oxidation-reduction potential in the solution is determined by the concentration correlation between hydrogen gas and water and the hydrogen ion concentration according to the Nernst equation, It cannot always be an indicator of reducibility. Furthermore, it cannot be a scavenger having a function of eliminating superoxide anion radicals, which are free radicals, by hydroxide and hydrogen gas. Similarly, in the anode-side electrolysis solution, an acid such as hydrochloric acid, oxygen gas, and hypochlorous acid are known as compositions, but it is obvious that hypochlorous acid plays a role in disinfecting action. It is. However, phenomena such as promotion of granulation are difficult to explain with these compositions, and it is necessary to find an independent system for the healing system.

【0007】生体内において細胞内のミトコンドリアが
酸素電子還元し、酸素の1電子還元であるスーパーオキ
サイドアニオンラジカルから4電子還元状態であるH2
Oまで連続的に反応が進行するが、その過程で水素イオ
ンや水酸イオンが消費される。これらのイオン種の内、
水酸イオンは、電子伝達系に関与しているとされてい
る。
In vivo, mitochondria in the cells undergo oxygen electron reduction, and H 2 in a four-electron reduced state is converted from a superoxide anion radical which is a one-electron reduction of oxygen.
The reaction proceeds continuously to O, and hydrogen ions and hydroxyl ions are consumed in the process. Of these ionic species,
Hydroxide ions are said to be involved in the electron transport system.

【0008】本発明は、上記事情に鑑みなされたもので
あり、その目的とするところは、電解質溶液を電気分解
することにより、両極側にて遊離のイオン種、すなわち
陰極では遊離の水酸イオン、陽極では遊離の水素イオン
を生成せしめることであり、Faraday の法則を利用しア
ルカリを構成している水酸イオンと、酸を構成している
水素イオンを中和滴定またはイオンの定量により、特に
陰極側に生成される陰極電解生成液を蒸留法または逆浸
透法あるいは両方の組合せにより遊離水酸イオンを含有
させた水を提供することである。
The present invention has been made in view of the above circumstances, and it is an object of the present invention to solve the above problem by electrolyzing an electrolyte solution to form free ionic species at both poles, ie, free hydroxyl ions at a cathode. This is to generate free hydrogen ions at the anode, and the neutralization titration or ion quantification of the hydroxyl ions constituting the alkali and the hydrogen ions constituting the acid is performed by Faraday's law. It is an object of the present invention to provide water containing free hydroxyl ions by a distillation method or a reverse osmosis method, or a combination of both, of a catholyte electrolysis solution produced on the cathode side.

【0009】また、一般に塩化ナトリウムのような電解
質は、水に溶解し陽イオンであるナトリウムイオンと陰
イオンである塩素イオンになり、0.1M程度の濃度で
は完全に解離していると同時にその活量係数が1に近似
できるので両イオンの濃度は同じである。また水酸化ナ
トリウムや塩酸のような場合も同様に陽イオンと陰イオ
ンの濃度も同じであり、前者は酸と後者は塩基と反応す
るが、遊離イオン種である遊離の水酸イオンや遊離の水
素イオンは酸あるいは塩基と反応せず、反対符号の遊離
イオン種かあるいは置換反応だけしか起こらず極めて安
定な遊離水酸イオン種を含む遊離水酸イオン水を提供す
ることができる。
In general, an electrolyte such as sodium chloride dissolves in water and becomes sodium ion as a cation and chloride ion as an anion. At a concentration of about 0.1 M, the electrolyte is completely dissociated at the same time. Since the activity coefficient can be approximated to 1, the concentrations of both ions are the same. Similarly, in the case of sodium hydroxide or hydrochloric acid, the concentrations of cations and anions are also the same.The former reacts with the acid and the latter reacts with the base, but the free ionic species free hydroxyl ion and free Hydrogen ions do not react with acids or bases, and only free ionic species of the opposite sign or only substitution reactions occur, so that free hydroxyl ionized water containing extremely stable free hydroxyl ionic species can be provided.

【0010】[0010]

【課題を解決するための手段】上記課題を解決するた
め、本発明に係わる遊離水酸イオンの製造法は、不活性
電極の陰極及び陽極を具備した電解槽に電解質溶液を入
れて前記陰極と陽極電極間に直流印加電流を流して、前
記電解質溶液を電解し、前記陰極側に遊離水酸イオンを
生成させ、次に、その電解生成液を前記電解槽から採取
して、蒸留法により蒸留するか、あるいは、逆浸透法に
より精製するか、あるいは、蒸留法と逆浸透法とを組み
合わせるかのいずれかにより電解質を除去し、遊離水酸
イオンを含有した遊離水酸イオン水を製造することを特
徴とする。
In order to solve the above-mentioned problems, a method for producing free hydroxyl ions according to the present invention comprises: placing an electrolytic solution in an electrolytic cell having a cathode and an anode of an inert electrode; A direct current is applied between the anode electrodes to electrolyze the electrolyte solution to generate free hydroxyl ions on the cathode side. Then, the electrolysis solution is collected from the electrolytic cell and distilled by a distillation method. Removing the electrolyte by either purifying by reverse osmosis or combining distillation and reverse osmosis to produce free hydroxyl ionized water containing free hydroxyl ions. It is characterized by.

【0011】また、不活性電極の陰極及び陽極と、それ
らの間に配置した隔膜とを具備した電解槽に電解質溶液
を入れて前記陰極と陽極電極間に直流印加電流を流し
て、前記電解質溶液を電解し、前記陰極側に遊離水酸イ
オンを生成させ、次に、その電解生成液を前記電解槽か
ら採取して、蒸留法により蒸留するか、あるいは、逆浸
透法により精製するか、あるいは、蒸留法と逆浸透法と
を組み合わせるかのいずれかにより電解質を除去し、遊
離水酸イオンを含有した遊離水酸イオン水を製造するこ
とを特徴とする。
Further, an electrolyte solution is put into an electrolytic cell having a cathode and an anode of an inert electrode and a diaphragm disposed therebetween, and a direct current is applied between the cathode and the anode electrode to cause the electrolyte solution to flow. To produce free hydroxyl ions on the cathode side, and then the electrolytic product is collected from the electrolytic cell and distilled by a distillation method, or purified by a reverse osmosis method, or The method is characterized in that the electrolyte is removed by any one of a combination of a distillation method and a reverse osmosis method to produce free hydroxyl ionized water containing free hydroxyl ions.

【0012】また、前記隔膜は荷電膜は、あるいは非荷
電膜かのいずれかであることを特徴とする。
[0012] Further, the invention is characterized in that the membrane is either a charged membrane or an uncharged membrane.

【0013】また、前記電解質溶液の濃度が10-4mo
l/lから飽和状態であり、陰陽両イオンの濃度が10
-4〜10-6mol/lであり、前記直流印加電流値が1
-1〜5Aの範囲であることを特徴とする。
Further, the concentration of the electrolyte solution is 10 −4 mo.
from 1 / l to the saturated state, the concentration of anion and cation is 10
-4 to 10 -6 mol / l, and the DC applied current value is 1
It is in the range of 0 -1 to 5A.

【0014】[0014]

【発明の実施の形態】本発明の遊離水酸イオンの製造法
による一実施の形態を以下に示す。遊離イオン種を含む
電解生成液は、先ず、図1に示すような電解槽1を使用
して電解を行なう。電解質溶液6は流入口6aから電解
槽1に入り、陰極2、陽極3、隔膜4の間を通り、それ
ぞれ陰極側及び陽極側生成液7、8となり、それらはそ
れぞれ陰極側流出口7a、陽極側流出口8aから流出す
る。陰極2と陽極3は不活性電極からなり、不活性電極
として白金電極を用い、電解質溶液6の電解助剤として
塩化ナトリウムを用い、陰極2、陽極3間に直流電源5
から印加し、それらの両極に遊離イオンを電解生成させ
たものである。次に、その電解生成液7は蒸留装置9で
蒸留し、電解質を除去した遊離水酸イオン水を生成す
る。
BEST MODE FOR CARRYING OUT THE INVENTION One embodiment of the method for producing free hydroxyl ions of the present invention will be described below. First, the electrolysis solution containing free ionic species is electrolyzed using an electrolytic cell 1 as shown in FIG. The electrolyte solution 6 enters the electrolytic cell 1 from the inlet 6a, passes between the cathode 2, the anode 3, and the diaphragm 4, and becomes the cathode-side and anode-side generated liquids 7 and 8, respectively, which are the cathode-side outlet 7a and the anode, respectively. It flows out from the side outlet 8a. The cathode 2 and the anode 3 are composed of inert electrodes, a platinum electrode is used as the inert electrode, sodium chloride is used as an electrolytic aid for the electrolyte solution 6, and a DC power source 5 is connected between the cathode 2 and the anode 3.
, And free ions are electrolytically generated at both electrodes. Next, the electrolysis product liquid 7 is distilled by the distillation apparatus 9 to generate free hydroxyl ionized water from which the electrolyte has been removed.

【0015】ここで、電解助剤としては1価−1価電解
質である塩化ナトリウムの他、塩化カリウムあるいは2
価−1価電解質である塩化カルシウムや塩化マグネシウ
ム等であればよく、また支持電解質である硫酸でもよ
い。不活性電極は、白金系電極ならばいかなる電極でも
よく、不可逆電極であることが絶対的条件である。また
隔膜4は陰イオン交換膜あるいは陽イオン交換膜のいず
れも採用することができる。更に、非荷電膜である中性
膜も採用できるが、荷電膜はイオン選択性をより高める
ことができるので中性膜よりも荷電膜の方が好ましい。
中性膜でも膜の構成ポアの小さいものならよい。
Here, as the electrolysis assistant, in addition to sodium chloride which is a monovalent monovalent electrolyte, potassium chloride or sodium chloride is used.
It may be calcium chloride, magnesium chloride, or the like, which is a monovalent monovalent electrolyte, or sulfuric acid, which is a supporting electrolyte. The inert electrode may be any electrode as long as it is a platinum-based electrode, and it is an absolute condition that it is an irreversible electrode. The diaphragm 4 may employ either an anion exchange membrane or a cation exchange membrane. Further, although a neutral membrane which is an uncharged membrane can be employed, a charged membrane is more preferable than a neutral membrane because a charged membrane can further enhance ion selectivity.
A neutral membrane may be used as long as the pores of the membrane are small.

【0016】遊離水酸イオンや遊離水酸イオンの生成
は、使用する電解質濃度が10-4mol/lから飽和状
態の範囲で可能であり、陰陽両イオンの遊離イオン濃度
は10-4〜10-2mol/lの範囲で生成可能である。
直流印加電流値は10-1〜5Aの範囲であれば遊離イオ
ンの生成は可能である。
The formation of free hydroxyl ions and free hydroxyl ions can be performed when the concentration of the electrolyte used is in the range of 10 -4 mol / l to a saturated state, and the free ion concentration of the anion and cation is 10 -4 to 10. It can be produced in the range of -2 mol / l.
Free ions can be generated if the DC applied current value is in the range of 10 -1 to 5A.

【0017】電解生成液の分析方法は、陰イオン交換膜
を用いた場合、陰極側では塩素イオンが陽極側に移動し
た量だけ減少し、ナトリウムイオンと水酸イオンで水酸
化ナトリウムを形成するので、中和滴定法により水酸イ
オンの量を定量することができる。またイオンクロマト
グラフ法により減少した塩素イオン量を定量してもよ
い。中和滴定法もイオンクロマトグラフ法も殆ど同じ精
度で定量できる。また遊離の水酸イオンと水酸化ナトリ
ウムの水酸イオンの総量は、Faraday の法則により電流
と時間の積をFaraday 定数で除することにより見積もる
ことができる。遊離の水酸イオンは水酸イオンの総量と
中和滴定法あるいはイオンクロマトグラフ法により定量
した量の差から求めることができる。陽極側においては
Faraday の法則により求めた水素イオンの総量と中和滴
定法あるいはイオンクロマトグラフより定量した水素イ
オン量との差から遊離の水素イオンが求められる。なお
陽極側では塩酸と次亜塩素酸が水素イオンとして定量で
きる。以下に両極側で起こる電極反応を示す。
According to the method for analyzing the electrolytic product, when an anion exchange membrane is used, the amount of chlorine ions on the cathode side decreases by the amount moved to the anode side, and sodium hydroxide and sodium ions form sodium hydroxide. The amount of hydroxyl ions can be determined by neutralization titration. Alternatively, the reduced amount of chloride ions may be quantified by ion chromatography. Neutralization titration and ion chromatography can be quantified with almost the same precision. The total amount of free hydroxide ion and sodium hydroxide can be estimated by dividing the product of current and time by Faraday's constant according to Faraday's law. Free hydroxyl ions can be determined from the difference between the total amount of hydroxyl ions and the amount determined by neutralization titration or ion chromatography. On the anode side
Free hydrogen ions are determined from the difference between the total amount of hydrogen ions determined by Faraday's law and the amount of hydrogen ions determined by neutralization titration or ion chromatography. On the anode side, hydrochloric acid and hypochlorous acid can be quantified as hydrogen ions. The electrode reactions occurring on both sides are shown below.

【0018】陰極側における反応 H2 O+e- → 1/2H2 +OH- (C1) (1) Na+ +OH- (C2) → NaOH (2) 但し、[OH- (C1) ],[OH- (C2) ]はそれぞれ総水
酸イオン濃度、水酸化ナトリウムの水酸イオン濃度を示
す。
Reaction on the cathode side H 2 O + e → 1/2 H 2 + OH (C1) (1) Na + + OH (C2) → NaOH (2) where [OH (C1) ], [OH ( C2) ] indicate the total hydroxide ion concentration and the hydroxide ion concentration of sodium hydroxide, respectively.

【0019】 [Cl- (C1) ]−[Cl(C2)]=[Cl- (C3) ] (3) 但し、[Cl- (C1) ]、[Cl(C2)]、[Cl- (C3)
はそれぞれ電解前の塩素イオン濃度、電解後の塩素イオ
ン濃度、陰極側から陽極側に移動した塩素イオン濃度を
示す。 [OH- (C2) ]=[Cl- (C3) ] (4)
[0019] [Cl - (C1)] - [Cl (C2)] = [Cl - (C3)] (3) where, [Cl - (C1)] , [Cl (C2)], [Cl - (C3 ) ]
Indicates the chloride ion concentration before electrolysis, the chloride ion concentration after electrolysis, and the chloride ion concentration moved from the cathode side to the anode side, respectively. [OH - (C2)] = [Cl - (C3)] (4)

【0020】陽極側における反応 1/2H2 O → 1/4O2 +H+ (a1) +e- (5) Cl- (al) → 1/2Cl2 +e- (6) 1/2Cl2 +H2 O → HOCl+H+ (a2) +e- (7) H+ (a2) +Cl- (a2) → HCl (8)[0020] The reaction at the anode side 1 / 2H 2 O → 1 / 4O 2 + H + (a1) + e - (5) Cl - (al) → 1 / 2Cl 2 + e - (6) 1 / 2Cl 2 + H 2 O → HOCl + H + (a2) + e - (7) H + (a2) + Cl - (a2) → HCl (8)

【0021】陰極側から陽極側に拡散移動した塩素イオ
ン量は両極側同量であることから [Cl- (a1) ]+[Cl(a2)]=[Cl- (C3) ] (9) 従って陽極では(5)、(6)の電極反応が進行し、
(5)、(8)により塩酸が生成される。
[0021] Since the amount of chlorine ions diffused moves from the cathode side to the anode side is a bipolar-side the same amount [Cl - (a1)] + [Cl (a2)] = [Cl - (C3)] (9) Therefore At the anode, the electrode reactions (5) and (6) proceed,
Hydrochloric acid is generated by (5) and (8).

【0022】遊離の水素イオン量は [H+ (a1) ]+[H+ (a2) ]−[HOCl]−[HCl] (10) [H+ (a1) ]+[H+ (a2) ]はFaraday の法則に従って
電流と電解時間の積をFaraday 定数で除した値となる。
The amount of free hydrogen ions is [H + (a1) ] + [H + (a2) ]-[HOCl]-[HCl] (10) [H + (a1) ] + [H + (a2) ] Is the value obtained by dividing the product of current and electrolysis time by the Faraday constant according to Faraday's law.

【0023】上記の方法で生成された電解生成液を蒸留
装置により蒸留するかあるいは逆浸透法により精製する
かあるいは蒸留法と逆浸透法を組み合わせてもよく、電
解質を除去し、遊離水酸イオンのみを含有した遊離水酸
イオン水とする。遊離水酸イオン水は、水のネットワー
クの中に取り込まれ水素結合をして水中に存在するので
一般的な分析法では分析できないのでアスコルビン酸で
中和反応させた後、スーパーオキサイドラジカルの消去
能を電子スピン共鳴法で分析する。コントロールとして
同質の純水を用い比較確認する。
The electrolysis solution produced by the above method may be distilled by a distillation apparatus, purified by a reverse osmosis method, or a combination of the distillation method and the reverse osmosis method. Free hydroxyl ionized water containing only Since free hydroxyl ion water is incorporated into the water network and undergoes hydrogen bonding and exists in the water, it cannot be analyzed by general analytical methods, so after neutralization with ascorbic acid, the ability to scavenge superoxide radicals Is analyzed by electron spin resonance. Compare and confirm using pure water of the same quality as a control.

【0024】[0024]

【実施例】本発明を実施例によって更に詳細に説明す
る。本発明はこれらの実施例に限定されない。実施例1 硬質塩化ビニールの電解槽中に陰イオン交換膜を使用
し、電極に白金電極を用い、陰極側と陽極側にそれぞれ
400mlの10-1Mの塩化ナトリウム溶液を入れ、
0.5Aの直流電流を印加し、3、5、7、9、11分
間それぞれ電解し、生成された電解液を中和滴定および
イオンクロマトグラフ法にて陰極側に生成された塩素イ
オンおよび水酸イオンの濃度を定量し、遊離の水酸イオ
ンを求めた。表1にその結果を示す。
The present invention will be described in more detail by way of examples. The present invention is not limited to these examples. Example 1 An anion exchange membrane was used in a rigid vinyl chloride electrolytic cell, a platinum electrode was used as an electrode, and 400 ml of a 10 -1 M sodium chloride solution was placed on each of a cathode side and an anode side.
A 0.5 A direct current is applied, and electrolysis is performed for 3, 5, 7, 9, and 11 minutes, respectively. The generated electrolyte is subjected to neutralization titration and ion chromatography to chlorine ion and water generated on the cathode side. The concentration of acid ions was quantified to determine free hydroxyl ions. Table 1 shows the results.

【0025】[0025]

【表1】遊離の水酸イオン濃度(濃度単位は10-3mole
s/400ml )
[Table 1] Free hydroxyl ion concentration (concentration unit is 10 -3 mole
s / 400ml)

【0026】9分間電解した陰極電解生成液400ml
を蒸留装置に入れ蒸留し、200ml蒸留した時点で終
了し、冷却した後イオンクロマトグラフでナトリムイオ
ンと塩素イオンの定量分析を行った。その結果コントロ
ールに用いた純水と同値となり、遊離の水酸イオン以外
のイオン類を除去したことを確認した。
400 ml of a cathodic electrolysis solution electrolyzed for 9 minutes
Was placed in a distillation apparatus and distilled, and the distillation was completed when 200 ml had been distilled. After cooling, quantitative analysis of sodium ions and chlorine ions was performed by ion chromatography. As a result, the value was the same as that of the pure water used for the control, and it was confirmed that ions other than free hydroxyl ions were removed.

【0027】更に遊離の水酸イオンを確認するため、蒸
留した陰極電解生成水100mlに5mlのL−アスコ
ルビン酸を入れ遊離のプロトンを生成した後、ヒポキサ
ンチン−キサンチンオキシダーゼ系によってできるスー
パーオキサイドの消去能を電子スピン共鳴装置により測
定した。尚コントロールには同質の純水を用いた。表2
にその結果を示す。
In order to further confirm free hydroxyl ions, 5 ml of L-ascorbic acid was added to 100 ml of distilled cathodic electrolysis water to generate free protons, followed by elimination of superoxide produced by the hypoxanthine-xanthine oxidase system. The performance was measured with an electron spin resonance apparatus. The control used was pure water of the same quality. Table 2
Shows the results.

【0028】[0028]

【表2】スーパーオキサイドの消去能(単位はunit/g) [Table 2] Superoxide erasing ability (unit is unit / g)

【0029】実施例2 実施例1で生成した電解時間7分の陰極電解生成液40
00mlを逆浸透法により処理した後、イオンクロマト
グラフでナトリムイオンと塩素イオンの定量分析を行っ
た。その結果コントロールに用いた純水と同値となり、
遊離の水酸イオン以外のイオン類を除去したことを確認
した。逆浸透法で処理した陰極電解生成水100mlに
5mlのL−アスコルビン酸を入れ遊離のプロトンを生
成した後、ヒポキサンチン−キサンチンオキシダーゼ系
によってできるスーパーオキサイドの消去能を電子スピ
ン共鳴装置により測定した。尚、コントロールには同質
の純水を用いた。表3にその結果を示す。
EXAMPLE 2 Cathodic electrolysis solution 40 generated in Example 1 for an electrolysis time of 7 minutes
After treating 00 ml by a reverse osmosis method, quantitative analysis of sodium ion and chloride ion was performed by ion chromatography. As a result, it becomes the same value as pure water used for control,
It was confirmed that ions other than free hydroxyl ions were removed. After 5 ml of L-ascorbic acid was added to 100 ml of cathodic electrolysis water treated by the reverse osmosis method to generate free protons, the elimination ability of superoxide produced by the hypoxanthine-xanthine oxidase system was measured by an electron spin resonance apparatus. In addition, the same pure water was used for the control. Table 3 shows the results.

【0030】[0030]

【表3】スーパーオキサイドの消去能(単位はunit/g) [Table 3] Elimination ability of superoxide (unit is unit / g)

【0031】実施例3 実施例1で生成した電解時間11分の陰極電解生成液4
000mlを蒸留し、かつ逆浸透法により処理した後、
イオンクロマトグラフでナトリムイオンと塩素イオンの
定量分析を行った。その結果コントロールに用いた純水
と同値となり、遊離の水酸イオン以外のイオン類を除去
したことを確認した。この蒸留し、かつ逆浸透法で処理
した陰極電解生成水100mlに5mlのL−アスコル
ビン酸を入れ遊離のプロトンを生成した後、ヒポキサン
チン−キサンチンオキシダーゼ系によってできるスーパ
ーオキサイドの消去能を電子スピン共鳴装置により測定
した。尚コントロールには同質の純水を用いた。表4に
その結果を示す。
Example 3 Cathode electrolysis solution 4 generated in Example 1 for an electrolysis time of 11 minutes
After distilling 000 ml and treating by reverse osmosis,
Quantitative analysis of sodium ion and chlorine ion was performed by ion chromatography. As a result, the value was the same as that of the pure water used for the control, and it was confirmed that ions other than free hydroxyl ions were removed. After 5 ml of L-ascorbic acid was added to 100 ml of the cathodic electrolyzed water treated by the reverse osmosis method to generate free protons, the elimination ability of superoxide by the hypoxanthine-xanthine oxidase system was measured by electron spin resonance. It was measured by the device. The control used was pure water of the same quality. Table 4 shows the results.

【0032】[0032]

【表4】スーパーオキサイドの消去能(単位はunit/g) [Table 4] Elimination ability of superoxide (unit is unit / g)

【0033】[0033]

【発明の効果】以上の通り本発明による遊離水酸イオン
の製造法によれば以下のような効果を奏する。 1)一定条件下で電解質溶液を電解することにより、陰
陽両極に遊離イオンを生成せしめ、遊離イオンは陽イオ
ンと陰イオンから構成される電解質溶液や酸や塩基と反
応せず、極めて安定であり、陰極電解生成液が生体内に
取り込まれた場合、反対符号の遊離イオンが存在しない
限り、フリーラジカルを含む活性酸素が局在する部位ま
で安定して到達し易く、スカーベンジャーとしての役割
を果たす。また生体内にアスコルビン酸が存在するとア
スコルビン酸の第3位と2位の位置にある水酸基の水素
と置換し、水素イオンを放出し、水素イオンとスーパー
オキサイドアニオンとが反応して不均化が起こり過酸化
水素を生成する。従って遊離水酸イオンはスーパーオキ
サイドディスムターゼ様の働きを示す。その結果、細胞
レベルの修復作用を促し、疾病を改善させることができ
る。また陽極電解生成液は遊離の水酸イオンを含有する
ため、コラーゲンの生成を促し創傷治癒に効果を発揮す
る。
As described above, the method for producing free hydroxyl ions according to the present invention has the following effects. 1) By electrolyzing the electrolyte solution under certain conditions, free ions are generated at the cathode and the anode. The free ions do not react with the electrolyte solution composed of cations and anions, acids or bases, and are extremely stable. When the cathodic electrolysis product is taken into a living body, it easily reaches a site where active oxygen containing free radicals is localized, as long as there is no free ion of the opposite sign, and plays a role as a scavenger. . In addition, when ascorbic acid is present in the living body, it displaces the hydrogen of the hydroxyl group at the 3rd and 2nd position of ascorbic acid, releases hydrogen ions, and reacts with hydrogen ions and superoxide anion to cause disproportionation. It produces hydrogen peroxide. Thus, the free hydroxide ion exhibits a superoxide dismutase-like action. As a result, a cell-level repair action can be promoted, and the disease can be improved. Further, since the anodic electrolysis solution contains free hydroxyl ions, it promotes collagen production and exerts an effect on wound healing.

【0034】2)遊離イオンは、電気分解を用いイオン
の拡散移動に伴ってわずかに解離している水分子が輸送
され電子として輸送されることによりエネルギー収支が
成立し、輸送されないで残ったイオンとして生成され
る。また電気化学的に反応が進行するので、化学量論的
に扱えることと、極めて簡便に行うことができ、尚かつ
安価に生成製造できるので、工業的規模でも容易に行う
ことができるという優れた効果を奏する。
2) The free ions are transported as water molecules, which are slightly dissociated with the diffusion transfer of the ions by electrolysis, and are transported as electrons, whereby an energy balance is established. Is generated as In addition, since the reaction proceeds electrochemically, it can be handled stoichiometrically and can be performed extremely easily, and can be produced and manufactured at low cost, so that it can be easily performed on an industrial scale. It works.

【0035】3)電解生成液中の電解助剤等の夾雑物を
蒸留法あるいは逆浸透法により除去し、遊離のイオンを
効率良く保持した遊離イオン水を簡便に製造することが
できる。また、本発明の遊離水酸イオンの製造法による
遊離イオン含有電解生成液は、精度を高くすることで医
薬品としても利用できる等の著効を有する。
3) Contaminants such as an electrolytic aid in the electrolysis solution are removed by a distillation method or a reverse osmosis method, and free ion water in which free ions are efficiently retained can be easily produced. Further, the free ion-containing electrolytic product solution produced by the method for producing free hydroxyl ions of the present invention has a remarkable effect such that it can be used as a drug by increasing the accuracy.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の一実施の形態である電解装置の構成を
説明する図である。
FIG. 1 is a diagram illustrating a configuration of an electrolytic device according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 電解槽 2 陰極 3 陽極 4 隔膜 5 直流電源 6 電解質溶液 7 陰極側電解生成液 8 陽極側電解生成液 9 蒸留装置 10 遊離水酸イオン水 DESCRIPTION OF SYMBOLS 1 Electrolyzer 2 Cathode 3 Anode 4 Diaphragm 5 DC power supply 6 Electrolyte solution 7 Cathode side electrolysis solution 8 Anode side electrolysis solution 9 Distillation apparatus 10 Free hydroxyl ion water

【手続補正書】[Procedure amendment]

【提出日】平成10年6月9日[Submission date] June 9, 1998

【手続補正1】[Procedure amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0017[Correction target item name] 0017

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0017】電解生成液の分析方法は、陰イオン交換膜
を用いた場合、陰極側では塩素イオンが陽極側に移動し
た量だけ減少し、ナトリウムイオンと水酸イオンで水酸
化ナトリウムを形成するので、中和滴定法により水酸イ
オンの量を定量することができる。またイオンクロマト
グラフ法により減少した塩素イオン量を定量してもよ
い。中和滴定法もイオンクロマトグラフ法も殆ど同じ精
度で定量できる。また遊離の水酸イオンと水酸化ナトリ
ウムの水酸イオンの総量は、Faradyの法則により
電流と時間の積をFarady定数で除した値と電流効
率の積から見積もることができる。また電解前の電解質
溶液を一定濃度の塩酸で酸性にし、一定濃度の水酸化ナ
トリウムで中和滴定した際の水酸化ナトリウムの消費量
[OHを遊離の水酸イオンを0とし、電解後の電
解生成溶液を同一の方法で同一のpHから水酸化ナトリ
ウムで中和した際の水酸化ナトリウムの消費量[O
cathodを求め、前者と後者の差、[O
cathod−[OHより電解による陰極
側に生成された遊離の水酸イオンを求めることができ
る。また陽極側における水素イオンの総量は、Fara
dyの法則により電流と時間の積をFarady定数で
除した値と電流効率の積から見積もることができる。ま
た電解前の電解質溶液を一定濃度の水酸化ナトリウムで
アルカリにし、一定濃度の塩酸で中和滴定した際の塩酸
の消費量[Hを遊離の水素イオンを0とし、電解
後の電解生成溶液を同一の方法で同一のpHから塩酸で
中和した際の塩酸の消費量[Hanodを求め、前
者と後者の差[Hanod−[Hより電解に
よる陽極側に生成された遊離の水素イオンを求めること
ができる。
According to the method for analyzing the electrolytic product, when an anion exchange membrane is used, the amount of chlorine ions on the cathode side decreases by the amount moved to the anode side, and sodium hydroxide and sodium ions form sodium hydroxide. The amount of hydroxyl ions can be determined by neutralization titration. Alternatively, the reduced amount of chloride ions may be quantified by ion chromatography. Neutralization titration and ion chromatography can be quantified with almost the same precision. Further, the total amount of free hydroxyl ions and sodium hydroxide ions of sodium hydroxide can be estimated from the product of the current efficiency and the value obtained by dividing the product of the current and the time by the Farady constant according to Farady's law. Further, the electrolyte solution before electrolysis is acidified with a certain concentration of hydrochloric acid, and the consumption amount of sodium hydroxide [OH ] 0 when neutralization titration is performed with a certain concentration of sodium hydroxide is set to 0 for free hydroxyl ions. Consumption of sodium hydroxide when the subsequent electrolysis solution is neutralized with sodium hydroxide from the same pH in the same manner [O
H ] catod is calculated , and the difference between the former and the latter, [O
From H ] cathod − [OH ] 0 , free hydroxyl ions generated on the cathode side by electrolysis can be determined. The total amount of hydrogen ions on the anode side is Fara
It can be estimated from the product of the current efficiency and the value obtained by dividing the product of the current and the time by the Farady constant according to dy's law. In addition, the electrolyte solution before electrolysis is made alkaline with sodium hydroxide of a certain concentration, and the consumption amount of hydrochloric acid [H + ] 0 when neutralized and titrated with a certain concentration of hydrochloric acid is set to 0 for free hydrogen ions. The consumption amount of hydrochloric acid [H + ] anod when the resulting solution was neutralized with hydrochloric acid from the same pH by the same method was determined, and the difference between the former and the latter [H + ] anod- [H + ] 0 was used to determine the anode by electrolysis. The free hydrogen ions generated on the side can be determined.

【手続補正2】[Procedure amendment 2]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0019[Correction target item name] 0019

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0019】 [Cl (C1)]−[Cl(C2)]=[Cl (C3)] (3) 但し、[Cl (C1)]、[Cl(C2)]、[Cl
(C3)]はそれぞれ電解前の塩素イオン濃度、電解
後の塩素イオン濃度、陰極側から陽極側に移動した塩素
イオン濃度を示す。 [OH (C2)]=[Cl (C3)] (4) 遊離の水酸イオン量は[OH(C1)×(電流効
率)−[OH(C2)=[OHcathod
[OHとなる。
[0019] [Cl - (C1)] - [Cl (C2)] = [Cl - (C3)] (3) where, [Cl - (C1)] , [Cl (C2)], [Cl
- (C3) ] respectively indicate the chloride ion concentration before electrolysis, the chloride ion concentration after electrolysis, and the chloride ion concentration moved from the cathode side to the anode side. [OH - (C2)] = [Cl - (C3)] (4) hydroxyl ions of the free is [OH -] (C1) × ( current efficiency) - [OH -] (C2 ) = [OH +] cathod
[OH ] becomes 0 .

【手続補正3】[Procedure amendment 3]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0022[Correction target item name] 0022

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0022】遊離の水素イオン量 {[H (a1)]+[H (a2)]}×(電流効率)−[HOCl]−[ HCl]=[H anod]−[H (10)Free hydrogen ion amount {[H + (a1) ] + [H + (a2) ]} × (current efficiency)-[HOCl]-[HCl] = [H + anod ]-[H + ] 0 (10)

───────────────────────────────────────────────────── フロントページの続き (72)発明者 花 岡 孝 吉 長野県上田市大字上田1041 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Takayoshi Hanaoka 1041 Ueda, Oaza, Ueda City, Nagano Prefecture

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 不活性電極の陰極及び陽極を具備した電
解槽に電解質溶液を入れて前記陰極と陽極電極間に直流
印加電流を流して、前記電解質溶液を電解し、前記陰極
側に遊離水酸イオンを生成させ、次に、その電解生成液
を前記電解槽から採取して、蒸留法により蒸留するか、
あるいは、逆浸透法により精製するか、あるいは、蒸留
法と逆浸透法とを組み合わせるかのいずれかにより電解
質を除去し、遊離水酸イオンを含有した遊離水酸イオン
水を製造することを特徴とする遊離水酸イオンの製造
法。
1. An electrolyte solution is placed in an electrolytic cell provided with a cathode and an anode of an inert electrode, and a direct current is applied between the cathode and the anode electrode to electrolyze the electrolyte solution. Generating acid ions, and then collecting the electrolytic product from the electrolytic cell and distilling it by a distillation method,
Alternatively, it is characterized in that it is purified by a reverse osmosis method, or the electrolyte is removed by either of a distillation method and a reverse osmosis method, to produce free hydroxyl ion water containing free hydroxide ions. Method for producing free hydroxyl ions.
【請求項2】 不活性電極の陰極及び陽極と、それらの
間に配置した隔膜とを具備した電解槽に電解質溶液を入
れて前記陰極と陽極電極間に直流印加電流を流して、前
記電解質溶液を電解し、前記陰極側に遊離水酸イオンを
生成させ、次に、その電解生成液を前記電解槽から採取
して、蒸留法により蒸留するか、あるいは、逆浸透法に
より精製するか、あるいは、蒸留法と逆浸透法とを組み
合わせるかのいずれかにより電解質を除去し、遊離水酸
イオンを含有した遊離水酸イオン水を製造することを特
徴とする遊離水酸イオンの製造法。
2. An electrolyte solution is placed in an electrolytic cell having a cathode and an anode of an inactive electrode and a diaphragm disposed therebetween, and a direct current is applied between the cathode and the anode to cause the electrolyte solution to flow. To produce free hydroxyl ions on the cathode side, and then the electrolytic product is collected from the electrolytic cell and distilled by a distillation method, or purified by a reverse osmosis method, or A method for producing free hydroxyl ions, comprising removing an electrolyte by one of a combination of a distillation method and a reverse osmosis method, and producing free hydroxyl ion water containing free hydroxyl ions.
【請求項3】 前記隔膜は荷電膜は、あるいは非荷電膜
かのいずれかであることを特徴とする請求項2記載の遊
離水酸イオンの製造法。
3. The method for producing free hydroxyl ions according to claim 2, wherein said diaphragm is either a charged membrane or an uncharged membrane.
【請求項4】 前記電解質溶液の濃度が10-4mol/
lから飽和状態であり、陰陽両イオンの濃度が10-4
10-6mol/lであり、前記直流印加電流値が10-1
〜5Aの範囲であることを特徴とする請求項1、2又は
3記載の遊離水酸イオンの製造法。
4. The concentration of the electrolyte solution is 10 −4 mol /.
1 to a saturated state, and the concentration of the anion and cation is 10 −4 to
10 -6 mol / l, and the DC applied current value is 10 -1
The method for producing free hydroxyl ions according to claim 1, 2 or 3, wherein the concentration is in the range of 5 to 5A.
JP36817197A 1997-12-27 1997-12-27 Production of free hydroxide ion Pending JPH11192485A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP36817197A JPH11192485A (en) 1997-12-27 1997-12-27 Production of free hydroxide ion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP36817197A JPH11192485A (en) 1997-12-27 1997-12-27 Production of free hydroxide ion

Publications (1)

Publication Number Publication Date
JPH11192485A true JPH11192485A (en) 1999-07-21

Family

ID=18491134

Family Applications (1)

Application Number Title Priority Date Filing Date
JP36817197A Pending JPH11192485A (en) 1997-12-27 1997-12-27 Production of free hydroxide ion

Country Status (1)

Country Link
JP (1) JPH11192485A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1101510A1 (en) * 1999-11-19 2001-05-23 Morisawa, Shinkatsu Condensate of superoxide anion radical abolisher, producing method thereof and superoxide anion radical abolisher powder

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1101510A1 (en) * 1999-11-19 2001-05-23 Morisawa, Shinkatsu Condensate of superoxide anion radical abolisher, producing method thereof and superoxide anion radical abolisher powder
US6500458B1 (en) 1999-11-19 2002-12-31 Shinkatsu Morisawa Condensate of SAR abolisher, producing method thereof, and SAR abolisher powder

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